NATURAL RUBBER BIOSYNTHESIS:
PERSPECTIVES FROM POLYMER CHEMISTRY
A Dissertation
Presented to
The Graduate Faculty of The University of Akron
In Partial Fulfillment
of the Requirements for the Degree
Doctor of Philosophy
Cheng Ching Kurt Chiang
December, 2013 NATURAL RUBBER BIOSYNTHESIS:
PERSPECTIVES FROM POLYMER CHEMISTRY
Cheng Ching Kurt Chiang
Dissertation
Approved: Accepted:
Advisor Department Chair Dr. Judit E. Puskas Dr. Coleen Pugh
Committee Member Dean of the College Dr. Abraham Joy Dr. Stephen Z. D. Cheng
Committee Member Dean of the Graduate School Dr. Matthew Becker Dr. George R. Newkome
Committee Member Date Dr. Chrys Wesdemiotis
Committee Member Dr. Peter Rinaldi
ii
ABSTRACT
Natural Rubber (NR) is an important strategic raw material for manufacturing a
wide variety of industrial products. NR has been mainly obtained from Hevea
brasiliensis. The USA is self-sufficient in the production of synthetic rubber while NR supply in USA is mainly imported from Southeast Asia. However, synthetic rubber cannot match the performance of imported Hevea NR. It is a matter of great concern that the USA is highly vulnerable to disruptions of NR supply because of a possible introduction of leaf blight into plantations as none of the trees in plantations across
Southeast Asia have resistance to blight.
Puskas et al. postulated that the biosynthesis of polyisoprenoids in general, and that of NR in particular, may proceed by a living carbocationic polymerization process.
“Natural living carbocationic polymerization” (NLCP) mechanism was proposed in terms of accepted polymer chemical formalism, i.e., initiation, propagation, and equilibria between active and dormant species. This thesis studied the fundamental steps of NR biosynthesis in two ways: 1) characterization of NR from stabilized latex and in vitro
biosynthesis; 2) addition of isoprene (IP) and other derivatives to shift the enzymatic
equilibrium of the terpenoid biosynthesis lifecycle. Synthetic initiators to be used in in
vitro NR biosynthesis system were prepared and characterized.
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For the first portion of this thesis, in vitro NR biosynthesis was studied using high
resolution size exclusion chromatography (HR-SEC). Then, various compounds such as
isoprene (IP) and amylene were introduced to the in vitro NR biosynthesis system. The rationale behind these studies was based on the terpenoid biosynthesis lifecycle. HR-
SEC, gravimetric analysis, in situ Raman spectroscopy and NMR spectroscopy were used to study scenarios where the equilibrium was disrupted by the introduction of foreign chemical compounds.
The second goal of this research was to design and synthesize a synthetic initiator for the future synthesis in vitro of a novel polyisobutylene-block-cis-1,4-polyisoprene
(PIB-b-NR) diblock copolymer. Two feasible synthetic pathways were developed to yield the target synthetic initiator: one by conventional syntheses and the other through an enzymatic pathway. The ultimate purpose of this synthetic initiator is to explore if the cis-prenyltransferase enzyme will recognize the compound and eventually apply this concept to novel terpenoids/NR in vitro. A seven-step synthetic strategy for the preparation of the PIB-NPP synthetic initiator is proposed and presented.
iv
DEDICATION
To my parents, Wei Ching and Li Chen Chiang for all their love and support.
v ACKNOWLEDGEMENTS
I would like to express my gratitude to my advisor Professor Judit E. Puskas for
her guidance and support throughout the course of this research. I would also like to
thank my graduate committee members Dr. Matthew L. Becker, Dr. Abraham Joy, Dr.
Chrys Wesdemiotis and Dr. Peter Rinaldi for their helpful comments and objective
criticisms. Also, I would like to thank Dr. Balaka Barkakaty for her extended amount of
her help and time.
I am grateful to Dr. Puskas’ team members for their collaboration and for providing useful feedback throughout this research. I would like to especially thank Dr.
Mustafa Yasin Sȩn, Dr. Elizabeth Foreman-Orlowski, Dr. Serap Hayat-Soytaş, Dr. Lucas
Dos Santos, and Dr. Andrey Malkovsky for helpful discussions about my research and laboratory techniques/instrumentations. I would also want to thank Dr. Colleen
McMahan, Dr. Wenshuang Xie, Dr. Alexi Sokolov and Dr. Alain Deffieux for their samples and insights.
I would like to acknowledge financial support by NSF-CHE#0616834 (GOALI) and the Goodyear Tire & Rubber Company.
Finally, it would have been impossible to write this dissertation without my family’s love and support especially from Dr. Ozlem Turkarslan and Dr. Yi-Hsin Weng.
vi TABLE OF CONTENTS
Page
LIST OF TABLES ...... xii
LIST OF FIGURES ...... xiv
CHAPTER
I. INTRODUCTION ...... 1
II. BACKGROUND ...... 7
2.1. Chemical Structure of Natural Rubber ...... 7
2.2. History of Natural Rubber ...... 13
2.2.1. Synthetic Polyisoprenes ...... 15
2.3. Natural Rubber Biosynthesis ...... 19
2.3.1. Rubber Producing Plants ...... 19
2.3.2. Anatomy of the Hevea NR Latex ...... 21
2.3.3. Biochemical Pathway of Natural Rubber Biosynthesis In Vivo ...... 22
2.3.4. Prenyltransferases ...... 28
2.3.5. Mechanism of Prenylation in Short Chain Isoprenoids ...... 29
2.3.6. Proposed Mechanism of Natural Rubber Biosynthesis: Natural Living Carbocationic Polymerization (NLCP) ...... 30
2.4. In Vitro Natural Rubber Biosynthesis ...... 34
2.5. In Vitro Biosynthesis Using Modified Synthetic Initiators ...... 40
vii 2.6. Biomimetic Polymerization of IP ...... 42
III. EXPERIMENTAL ...... 46
3.1. Materials ...... 46
3.1.1. Preparation of Washed Rubber Particles (WRP) ...... 47
3.2. Procedures ...... 48
3.2.1. In Vitro Natural Rubber Biosynthesis (Hevea WRP) ...... 48
3.2.1.1. Small Scale Synthesis (USDA) ...... 48
3.2.1.2. Large Scale Synthesis (USDA) ...... 49
3.2.1.3. “Bioemulative” Experiments Using Synthetic Isoprene with WRP-3 (USDA) ...... 49
3.2.2. Experiments with IAC40 Latex ...... 50
3.2.2.1. Solids Content Determination for Latex and WRP ...... 50
3.2.2.2. In Situ Raman Monitoring ...... 50
3.2.2.3. Micro-Raman Spectroscopy ...... 51
3.2.2.4. Experiments under CO2 Atmosphere ...... 52
3.2.2.5. “Bioemulative” Experiments Using Deuterated Isoprene ...... 53
3.3. Synthesis of Macroinitiator ...... 54
3.3.1. Synthesis of Protected Nerol (PN, product 2) ...... 54
3.3.2. Synthesis of Protected Nerol-OH (PN-OH, product 3) ...... 54
3.3.3. Synthesis of Protected Nerol Tosylate (PN-Ts, product 4) ...... 55
3.3.4. Synthesis of Polyisobutylene-Protected Nerol (PIB-PN, product 5) ...56
3.3.5. Synthesis of Polyisobutylene-Nerol (PIB-Nerol, product 6) ...... 57
3.3.6. Synthesis of Polyisobutylene-Nerol-Bromide (PIB-Nerol-Br, product 7) ...... 57
3.3.7. Synthesis of Tris(tetra-n-butylammonium) Hydrogen Pyrophosphate [(NBu4)3HP2O7] ...... 57
viii 3.3.8. Synthesis of Nerol-PP (Model Reaction for Product 8) ...... 58
3.3.9. Synthesis of Protect Nerol-Divinyl Adipate (PN-DVA, Product 9) ....58
3.3.10. Synthesis of Trimethyl Pentyl Chloride (TMPCl, Product 10) ...... 59
3.3.11. Synthesis of Allyl Trimethyl Pentane (TMP-allyl, Product 11) ...... 59
3.3.12. Synthesis of Trimethyl Pentane-OH (TMP-OH, Product 12) ...... 60
3.3.13. Synthesis of Protected Nerol-Divinyl Adipate-Trimethyl Pentane (PN-DVA-TMP, Product 13) ...... 60
3.3.14. Synthesis of Nerol-Divinyl Adipate-Trimethyl Pentane (Nerol-DVA-TMP, Product 14) ...... 61
3.3.15. Synthesis of Nerol-Bromide-Divinyl Adipate-Trimethyl Pentane (Nerol-Br-DVA-TMP, Product 15) ...... 61
3.3.16. Synthesis of Nerol-Pyrophosphate-Divinyl Adipate-Trimethyl Pentane (Nerol-PP-DVA-TMP, Product 16) ...... 62
3.3.17. Synthesis of Nerol-P(O)(OEt)2 (Model Reaction for Phosphorylation) ...... 62
3.3.18. Synthesis of Nerol-P(O)(OEt)2-DVA-TMP (Product 15) ...... 63
3.3.19. Synthesis of Nerol-PP-DVA-TMP (Product 16) ...... 63
3.4. Laboratory Techniques and Instrumentation ...... 64
3.4.1. Air-free Technique ...... 64
3.4.2. Thin Layer Chromatography (TLC) ...... 64
3.4.3. Column Chromatography ...... 65
3.4.4. Size Exclusion Chromatography (SEC) ...... 66
3.4.5. NMR Sample Preparation ...... 67
3.4.6. 1H NMR Procedure ...... 68
3.4.7. 13C NMR Procedure ...... 68
3.4.8. Gas Chromatography (GC) ...... 68
ix 3.4.9. Matrix Assisted Laser Desorption/Ionization Time-of-Flight Mass Spectrometry (MALDI-ToF MS) ...... 69
3.4.10. Electrospray Ionization Mass Spectrometry (ESI-MS) ...... 69
IV. RESULTS AND DISCUSSION ...... 71
4.1. In Vitro Natural Rubber Biosynthesis ...... 71
4.1.1. Monitoring the Growth of in vitro Natural Rubber by High- Resolution Size Exclusion Chromatography (HR-SEC) ...... 71
4.2. Substitution of the Isopentenyl Pyrophosphate (IPP) Monomer with Synthetic Isoprene (IP) ...... 82
4.2.1. Monitoring the Effects of IP in in vitro Natural Rubber Biosynthesis. .83
4.2.2. Incubation of Synthetic D-IP with Hevea Latex...... 102
4.2.3. In Vitro NR Biosynthesis under CO2 Atmosphere...... 108
4.2.4. In Vitro NR Biosynthesis in the Presence of Amylene ...... 111
4.3. In Situ Micro-Raman Monitoring of In Vitro Natural Rubber (NR) Biosynthesis ...... 113
4.3.1. Raman Monitoring of In Vitro NR Biosynthesis Between Glass Slides ...... 113
4.3.2. Raman Monitoring of In Vitro NR Biosynthesis with Micro- Cavity Slides ...... 115
4.3.3. Raman Monitoring in Sealed Silanized Vials ...... 116
4.3.4. Raman Monitoring with Deuterated-Isoprene (D-IP) ...... 124
4.3.5. Raman Monitoring CO2 Atmosphere ...... 124
4.3.6. Effect of Addition on Latex Particle Size ...... 126
4.4. Macroinitiator Synthesis ...... 128
4.4.1. Synthesis of Protected Nerol (PN, Product 2) ...... 131
4.4.2. Synthesis of Protected Nerol-OH (PN-OH, Product 3) ...... 134
4.4.3. Synthesis of Protected Nerol Tosylate (PN-Ts, Product 4) ...... 136
x 4.4.4. Synthesis of Polyisobutylene Protected Nerol (PIB-PN, Product 5) .138
4.4.5. Deprotection of PIB-PN to PIB-Nerol (Product 6) ...... 142
4.4.6. Synthesis of Polyisobutylene-Nerol-Bromide (PIB-Nerol-Br, Product 7) ...... 144
4.4.7. Synthesis of Nerol Pyrophosphate (Nerol-PP, Model Reaction for Product 8) ...... 146
4.4.8. Synthetic Stretegy to Yield Macroinitiator Using Enzyme Catalysis ...... 147
4.4.9. Synthesis of Protected Nerol-Divinyl Adipate (PN-DVA, Product 9) ...... 149
4.4.10. Synthesis of TMP-OH (Product 12, PIB dimer) ...... 153
4.4.11. Synthesis of PN-DVA-TMP (Product 13) ...... 159
4.4.12. Synthesis of Nerol-DVA-TMP (Product 14) ...... 162
4.4.13. Synthesis of Nerol-Br-DVA-TMP (Product 15) ...... 165
4.4.14. Synthesis of Nerol-PP-DVA-TMP (Product 13) (Chen’s Method) ..167
4.4.15. Synthetic scheme to yield Nerol-OPP-DVA-TMP (Product 16) (Coates’Method) ...... 169
4.4.16. Synthesis of Nerol-OP(O)(OEt)2 (Model Reaction) ...... 170
4.4.17. Synthesis of Nerol-PP (Model Reaction) ...... 174
4.4.18. Synthesis of Nerol-OP(O)(OEt)2-DVA-TMP (Product 15) ...... 176
4.4.19. Synthesis of Nerol-PP-DVA-TMP (Product 16) ...... 179
V. CONCLUSIONS ...... 185
REFERENCES ...... 188
APPENDIX ...... 201
xi LIST OF TABLES
Table Page
2.2.1 Microstructures in synthetic PIPs ...... 15
4.1.1 HR-SEC data of WRP-1...... 75
4.1.2 Approximate MW of peaks 1L to 5L from HR-SEC...... 78
4.1.3 Gravimetric analysis of WRP-3/24...... 80
4.1.4 Gel fraction analysis of WRP-3 and WRP-3/24 ...... 80
4.1.5 SEC data of WRP-3 and WRP-3/24 ...... 81
4.2.1 Experimental conditions for WRP-3 with IP ...... 83
4.2.2 Gravimetric analysis summary for experiments with WRP-3 ...... 83
4.2.3a IAC40 latex solid content determination by freeze drying ...... 86
4.2.3b IAC40 WRP solid content determination by freeze drying ...... 86
4.2.4a Solid content of IAC40 latex after washing the coagulated rubber ...... 86
4.2.4b Solid content of IAC40 WRP after washing the coagulated rubber ...... 86
4.2.5a Solid content of IAC40 latex obtained by precipitation in methanol ...... 87
4.2.5a Solid content of IAC40 WRP obtained by precipitation in methanol ...... 87
4.2.6 Summary gravimetric data of in vitro NR samples ...... 89
4.2.7 Gel content of in vitro NR samples ...... 90
4.2.8 High and low MW parts of the soluble fractions obtained from the IAC40 latex and WRP ...... 92
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4.2.9a SEC analysis of the soluble fractions obtained from IAC40 latex before and after incubation with IP ...... 94
4.2.9b SEC analysis of the soluble fractions obtained from IAC40 WRP before and after incubation with IP ...... 94
4.2.10 Gravimetric summary of D-IP experiments ...... 106
4.2.11 Gravimetric analysis of in vitro NR biosynthesis under CO2 atmosphere ...... 109
4.2.12 Gel content of in vitro NR samples ...... 109
4.2.13 SEC analysis of the soluble fractions obtained from IAC40 latex/WRP before and after incubation with IP in CO2 ...... 111
4.2.14 Gravimetric summary for Amylene experiments ...... 112
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LIST OF FIGURES
Figure Page
2.1.1 DL-limonene (a) and isoprene (b) ...... 7
2.1.2 Suggested building blocks of NR before (a) and after (b) 1910 ...... 8
2.1.3 Chemical structure of NR. Head (ω) and end group (α) structure is not proven ...... 9
2.1.4 13C NMR spectrum of NR from Hevea (a) and Guayule (b) ...... 10
2.1.5 13C NMR spectrum of NR from L. volemus ...... 11
2.1.6 Deproteinization by treatment with 1~2% ethanol. (DMAPP denotes dimethylallyl pyrophosphate, FPP denotes Farnesyl pyrophosphate.) ...... 12
2.2.1 PIP microstructures. *the cyclics shows an example of C15, other cyclics may occur ...... 16
2.2.2 NMP of IP using 2,2,5-trimethyl-4-phenyl-3-azahexane-3oxy-nitroxide as initiator ...... 17
2.3.1 Examples of rubber producing plants ...... 20
2.3.2 Visualization of NR particles and its structure ...... 21
2.3.3 Structure of isopentenyl pyrophosphate IPP at pH = 7.4 ...... 22
2.3.4 Terpenoids biosynthesis cycle ...... 24
2.3.5 Synthesis of NR in H. brasiliensis. OPP stands for the pyrophosphate end-group and HOPP represents pyrophosphoric acid ...... 25
xiv
2.3.6 Structure of the allylic oligoisoprene pyrophosphates. DMAPP: dimethyl allyl pyrophosphate, GPP: geranyl pyrophosphate, FPP: farnesyl pyrophosphate, GGPP: geranylgeranyl pyrophosphate ...... 26
2.3.7 Biochemical representation of rubber biosynthesis ...... 27
2.3.8 A scheme of the active sites in avian trans-prenyltransferase. The oval represents a large motive proposed to stop chain growth ...... 28
2.3.9 The mechanism of terpenoid biosynthesis proven by Poulter et al ...... 30
2.3.10 Proposed NLCP mechanism of NR biosynthesis ...... 31
2.3.11 Yokozawa’s concept of chain-growth polycondensation ...... 32
2.3.12 Attempted “bio-inspired” synthesis of cis-1,4-polyisoprene. (The resulting polymer was in the trans conformation) ...... 33
2.4.1 Lineweaver-Burk Plot of IPP concentration vs. reaction velocity (V) in the determination of the enzymatic activity of Guayule WRP ...... 35
2.4.2 SEC trace of Hevea BF (dashed line) and in vitro NR (solid line) ...... 36
2.4.3 in vitro guayule NR biosynthesis ...... 38
2.4.4 Experimental MW results from Cornish et al.’s in vitro NR system for three types of WRPs (Fig tree, Guayule, and Hevea) a) 0.25 µM FPP, b) 2.5 µM FPP ...... 39
2.5.1 Chemical structure of DATFP-GPP ...... 41
2.5.2 Chemical structure of di-isobutylene-neryl pyrophosphate ...... 42
2.6.1 Biomimetic initiation of IP polymerization from Puskas et al ...... 43
2.6.2 Possible carbocationic polymerization pathways for IPOH ...... 44
2.6.3 Chemical scheme of cationic polymerization of IP with 1-(4-methoxyphenyl) ethanol as the initiator and B(C6F5)3 as the co-initiator .....45
3.2.1 Experimental set-up for the in situ Raman measurements ...... 51
3.2.2 Micro-Raman instrumentation in the Sokolov lab: a) before the experiment b) during in situ monitoring ...... 52
xv
3.2.3 Methodology to exchange the atmosphere within the closed vial ...... 53
3.4.1 High resolution SEC system at Puskas Lab ...... 67
4.1.1 Micro-well plates in which in vitro NR biosyntheses are performed ...... 72
4.1.2 An example micro-well and its constituents a) during and b) after incubation ...... 73
4.1.3 Enzyme activity measurement of RRIM 600 WRP using 14C IPP (USDA) ...... 73
4.1.4 SEC RI trace of WRP-1 ...... 74
4.1.5 Conformation Plot of WRP-3 ...... 75
4.1.6 SEC of WRP-1, WRP-1/5 and WRP-1/24. High MW region a) LS trace, b) RI trace ...... 77
4.1.7 SEC RI trace of WRP-1 and WRP-1/24. Low MW region ...... 77
4.1.8 MALDI-ToF spectrum of fractionated low MW Hevea NR (H600 clone) ...... 79
4.1.9 SEC traces of WRP-3 before and after incubation (a) RI traces of low MW region, (b) RI traces of high MW region ...... 81
4.2.1 Enzyme activity measurement using 14C-labelled IPP (USDA) ...... 85
4.2.2 Zoomed SEC RI chromatograms of the soluble fractions from IAC40 and WRP for comparison: a) high MW region, b) low MW region ...... 91
4.2.3 SEC RI trace of KC_092309_L_IP1 and starting latex ...... 93
4.2.4 Difference between (a) least square fit (unmodified) and (b) least absolute residual fit (modified) ...... 95
4.2.5 1H NMR (500 MHz) spectrum of KC_092309_L_IP1: 0-3.5 ppm region (Concentration: 10 mg/mL, 128 scans, d1 = 10 sec, Pulse angle = 90o, o T = 25 C, Solvent: toluene-D8.) ...... 97
4.2.6 1H NMR (500 MHz) spectrum of KC_092309_L_IP1: 3.75-7.5 ppm region (Concentration: 10 mg/mL, 128 scans, d1 = 10 sec, o o Pulse angle = 45 , T = 25 C, Solvent: toluene-D8.) ...... 97
xvi
4.2.7 13C NMR spectrum of KC_092309_L_IP1: 0-50 ppm region. (Concentration: 20 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: Chloroform-D.) ...... 98
4.2.8 13C NMR spectrum of KC_092309_L_IP1: 100-150 ppm region (Concentration: 20 mg/mL, 10,000 scans, d1 = 10s, Pulse Angle = 90o, T = 25°C, Solvent: Chloroform-D.) ...... 99
4.2.9 13C NMR (125 MHz) spectrum of KC_100909_L_IP5: 0-50 ppm region (Concentration: 50 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6.) ...... 100
4.2.10 13C NMR (125 MHz) spectrum of KC_100909_L_IP5: 100-155 ppm region (Concentration: 50 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6.) ...... 100
4.2.11 13C NMR (125 MHz) spectrum of KC_102109_W_IP8: 0-50 ppm region (500 MHz Concentration: 60 mg/mL, 10,000 scans, d1 = 10s, o Pulse angle = 90 , T = 25°C, Solvent: benzene-D6.) ...... 101
4.2.12 13C NMR (125 MHz) spectrum of KC_102109_W_IP8: 95-155 ppm region (Concentration: 60 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6.) ...... 102
4.2.13 Comparison of 1H NMR spectra of IP (red) and D-IP (black) (300 MHz, Concentration: 20 mg/mL, 32 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 103
4.2.14 Comparison of the 13C NMR spectra of IP (red) and D-IP (black) (300 MHz, concentration: 20 mg/mL, 32 scans, d1 = 10s, o Pulse angle = 90 , T = 25°C, Solvent: benzene-D6.) ...... 104
4.2.15 GC chromatograms of IP (red) and D-IP (black) ...... 105
4.2.16 13C NMR spectra (500 MHz) of the D-IP experimental series, 091610_D-IP_latex 2 (top), 092910_L_IP1_50D-IP_50IP (middle) and 092910_L_100IP (bottom), 0-140 ppm region. 10,000 scans, o d1 = 10s, Pulse angle = 90 , Solvent: benzene-D6, (Concentration: 15 mg/mL for KC091610_L_IP1(100D-IP) and 50 mg/mL for both KC092910 experiments.) ...... 107
4.2.17 SEC comparison RI traces of KC_102709_Latex_IAC40 and KC_121109_L_IP1(CO2/50X)...... 110
xvii
4.2.18 SEC comparison RI traces of KC120909_IAC40_WRP and KC121409_W_IP3 (CO2/50X)...... 110
4.2.19 Chemical structure of amylene...... 111
4.2.20 SEC comparison RI traces of 102709_Latex and KC_101510_L_Amy1 observed after incubation of IAC40 NR latex with amylene. The other two experiments (KC101510_L_Amy2 and KC101510_L_Amy3, not shown) showed similar results with KC101510_L_Amy1 with no changes in the SEC traces...... 112
4.3.1 Signals attributed to the C=C Raman-active vibrations in PIP and IP (Isoprene: liquid IP with stabilizer; Mixed sample: WRP RRIM600+IP 2/1 (w/w))...... 114
4.3.2 The schematics of the bottle illuminated by the Raman beam...... 117
4.3.3 Fluorescence problems illustrated for KC_092309_L_IP1 with 80X objective (092309_L_WRP: 0.5340g IAC40 latex, 0.1022g IP, 24h, RT) ...... 118
4.3.4 Raw spectra for a sequence of data points of KC_102109_W_IP8 (10 min between each spectra, 0.5079g IAC40 WRP, 0.1022g IP, 24h, RT.) ...119
4.3.5 Normalized PIP formation plots for two repeat experiments using 50X. objective (KC_110509_WRP_IP9: 0.5028g WRP, 0.1022g IP, 24h, RT. KC_120209_WRP_IP13: 0.5097g WRP, 0.1021g IP, 24h, RT.) ...... 120
4.3.6 Normalized PIP formation plots for two repeat experiments with 50X objective with error bars. (KC_102309_WRP_IP8: 0.5079g WRP, 0.1022g IP, 24h, RT. KC_111209_WRP_IP10: 0.5843g WRP, 0.1022g IP, 24h, RT.) ...... 121
4.3.7 Normalized IP consumption plots for three repeat experiments with 50X objective (103209_WRP_IP8: 0.5079g WRP, 0.1022g IP, 24h, RT 110509_WRP_IP9: 0.5028g WRP, 0.1022g IP, 24h, RT 111209_WRP_IP10: 0.5843g WRP, 0.1022g IP, 24h, RT.) ...... 122
4.3.8 Raman monitoring of in vitro NR biosynthesis. (KC_102109_WRP_IP8: 0.5079 g IAC40 WRP, 0.1021 g IP, 24 hrs, RT) ...... 123
4.3.9 Raman monitoring of KC091710_L_IP3 (100DIP) ...... 124
4.3.10 PIP growth comparison between WRP experiments and KC_121409_W_IP3 (CO2/50X) 0.5085 g IAC40 WRP, 0.102 g IP, o 24 hrs under CO2 atmosphere, at 25 C, color: yellow ...... 125
xviii
4.3.11 PIP growth comparison between KC_092909_L_IP4 and KC_120809_L_IP1 (CO2/50X), 0.6406 g IAC40 Latex, 0.130 g IP, 24 hrs under CO2 atmosphere at 25 C, color: yellow ...... 126
4.3.12 Optical images of Hevea latex particles (Neotex HA) casted on a flat glass slide...... 127
4.3.13 Size distribution of Neotex HA latex particles...... 127
4.4.1 Synthetic strategy to produce PIB-NPP macroinitiator PPTs = pyridinium p-toluenesulfonate; DHP = dihydropyran; NBS = N-bromosuccinimide; TsCl = tosyl chloride; IPA = isopropyl alcohol ...130
4.4.2 1H NMR spectrum of nerol. (300 MHz, 32 scans, d1 = 1s, Pulse angle = 45o , T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.2) ...... 132
4.4.3 1H NMR spectrum of PN (product 2). (300 MHz, 64 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.3) ...... 133
4.4.4 13C NMR spectrum of PN (product 2). (500 MHz, 5,000 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.4) ...... 134
4.4.5 1H NMR spectrum of PN-OH (product 3). (300 MHz, 64 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.5) ...... 135
4.4.6 13C NMR spectrum of PN-OH (product 3). (300 MHz, 5,000 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.6) ...... 136
4.4.7 1H NMR spectrum of PN-Ts (product 4). (300 MHz, 64 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.7)...... 137
4.4.8 13C NMR spectrum of PN-Ts (product 4) (500 MHz, 5,000 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.8) ...... 138
4.4.9 1H NMR spectrum of starting PIB-OH (#16) (300 MHz, 128 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.9) ...... 139
4.4.10 13C NMR spectrum of starting PIB-OH (#16) (300 MHz, 5,000 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.10) ...... 140
4.4.11 1H NMR spectrum of PIB-PN (product 5) (300 MHz, 128 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.11) ...... 141
xix
4.4.12 13C NMR spectrum of PIB-PN (product 5). (500 MHz, 6,400 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.12) ...... 142
4.4.13 1H NMR spectrum of PIB-Nerol (product 6) (300 MHz, 128 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.13) ...... 143
4.4.14 13C NMR spectrum of PIB-Nerol (product 6) (300 MHz, 5,000 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.14) ...... 144
4.4.15 1H NMR spectrum of PIB-Nerol-Br (product 7) (300 MHz, 128 scans, d1 = 10s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.15) ...... 145
4.4.16 13C NMR spectrum of PIB-Nerol-Br (product 7) (500 MHz, 4,600 scans, d1 = 10s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.16) ...... 146
4.4.17 1H NMR spectrum of Nerol-PP(model compound of product 8) (300 MHz, 128 scans, d1 = 5s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 147
4.4.18 Enzyme-catalyzed synthetic scheme to yield Nero-PP-DVA-TMP ...... 149
4.4.19 1H NMR spectrum of PN-DVA (product 9). (300 MHz, 64 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 151
4.4.20 13C NMR spectrum of PN-DVA (product 9). (500 MHz, 2,800 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 152
4.4.21 ESI-MS spectrum of PN-DVA (product 9). (solvent: THF, cationizing agent: NaTFA, sample/salt: 100/1 (v/v)) ...... 153
4.4.22 Synthetic scheme to yield TMP-OH (PIB dimer) ...... 154
4.4.23 1H NMR spectrum of TMP-1. (300 MHz, 32 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 155
4.4.24 1H NMR spectrum of TMPCl. (300 MHz, 64 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 156
4.4.25 1H NMR spectrum of TMP-allyl. (300 MHz, 32 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 157 4.4.26 1H NMR spectrum of TMP-OH. (300 MHz, 32 scans, d1 = 1s, Pulse angle = 45o, T = 25°C, Solvent: chloroform-D.) ...... 158
xx
4.4.27 ESI-MS of TMP-OH. (solvent: Methanol, cationizing agent: NaTFA, sample/salt: 100/1 (v/v)) ...... 159
4.4.28 1H NMR spectrum of PN-DVA-TMP (product 13). (300 MHz, 32 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.28) ...... 160
4.4.29 13C NMR spectrum of PN-DVA-TMP (product 10). (125 MHz, 3,600 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.29) ...... 161
4.4.30 ESI-MS spectrum of PN-DVA-TMP (product 10). (solvent: THF, cationizing agent: NaTFA, sample/salt: 100/1 (v/v)) ...... 162
4.4.31 1H NMR spectrum of Nerol-DVA-TMP (product 14). (300 MHz, 64 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.31) ...... 164
4.4.32 13C NMR spectrum of Nerol-DVA-TMP (product 14). (75 MHz, 3600 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.32) ...... 165
4.4.33 1H NMR spectrum of Nerol-Br-DVA-TMP (product 15). (300 MHz, 64 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.33) ...... 166
4.4.34 13C NMR spectrum of Nerol-Br-DVA-TMP (product 15). (75 MHz, 3600 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.34) ...... 167
4.4.35 31P NMR spectrum of diethyl chlorophosphate. Bu denotes n-butyl group (300 MHz, 300 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 168
4.4.36 Synthetic scheme to yield Nero-PP-DVA-TMP adapted from Coates et al ...... 170
4.4.37 31P NMR spectrum of diethyl chlorophosphate. (300 MHz, 400 scans, d1 = 2s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 171
31 4.4.38 P NMR spectrum of crude product of Nerol-P(O)(OEt)2.(300 MHz, 400 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 172
31 4.4.39 P NMR spectrum of Nerol-P(O)(OEt)2. (after column) (300 MHz, 400 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 173
xxi
1 4.4.40 H NMR spectrum of Nerol-P(O)(OEt)2. (300 MHz, 64 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.40) ...... 174
4.4.41 31P NMR spectrum of Nerol-PP. (crude, Bu denotes n-Butyl) (300 MHz, 400 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 175
4.4.42 ESI-MS spectrum of Nerol-PP. (Negative Mode. solvent: acetonitrile, ionizing agent: n/a)………………………………………………………………………176
31 4.4.43 P NMR spectrum of Nerol-OP(O)(OEt)2-DVA-TMP. (300 MHz, 400 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 177
1 4.4.44 H NMR spectrum of Nerol-P(O)(OEt)2-DVA-TMP. (300 MHz, 64 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.44) ...... 178
4.4.45 31P NMR spectrum of Nerol-PP-DVA-TMP. (product 16) (300 MHz, 400 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D.) ...... 180
4.4.46 1H NMR spectrum of Nerol-PP-DVA-TMP. (product 16) (300 MHz, 64 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.46) ...... 181
4.4.47 13C NMR spectrum of Nerol-PP-DVA-TMP (product 16). (300 MHz, 64 scans, d1 = 1s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D. Appendix: B.4.4.47) ...... 182
+ 4.4.48 ESI-MS spectrum of Nerol-PP-TMP-DVA. Bu4N denotes tetra-n-butylammonium ion.(Solvent: acetonitrile, cationizing agent: n/a) ...... 184
xxii
CHAPTER I
INTRODUCTION
Plants are present in all aspects of everyday life; they provide food, produce the oxygen that organisms breathe, and serve as raw materials in many of our clothes, buildings, drugs and perfumes. Despite the diversity of plants, human life relies only on relatively few species. Even though the Olmec, who are often referred to as the “rubber people”, first discovered Natural Rubber (NR) around 1,600 B.C.1, it was not until 1839 that rubber had its first practical application in the industry when Charles Goodyear accidentally dropped rubber and sulfur on a hot stovetop, causing it to be resilient like leather while retaining elasticity.2, 3 NR is a critical and strategic industrial raw material
for manufacturing a wide variety of products, ranging from medical devices and personal
protective equipment to aircraft tires. Car tires are made from 12-14 different rubbers, of
which up to 50% of the rubber used can be NR. Aircraft and race tires contain only NR.2
It is known that more than 2,500 plant species produce NR; however, NR
harvested from a single species, Hevea brasiliensis (Brazilian rubber tree) is the most
important commercial source.4 Today 85% of the USA NR supply is imported from
Southeast Asia and the remaining 15% comes from the South and Central Americas.5, 6 In
2006, the total global production of natural rubber was ~9 million metric tons.7
1
The US is highly vulnerable to disruptions of NR supply such as a possible
introduction of leaf blight into plantations.2 None of the trees in plantations across
Southeast Asia have resistance to blight. South American leaf blight (SALB) is a fungal disease common to rubber trees caused by the endemic fungus Microcyclus ulei, an
ascomycota (sac fungi) that spreads by spores.7 Currently, SALB is restricted to South
and Central Americas due to strict control over air traffic and freight shipments from
South America to Southeast Asia. However, future intercontinental passenger flights
between Southeast Asia and South America can be detrimental to the rubber plantations
if not controlled properly.
The rapid development of Brazil in the late 19th Century was similar to the Gold
Rush in Alaska. The Industrial Revolution increased the production of automobiles and
spread electricity, which raised the demand of NR significantly and NR became a global
commodity.8 Immigrants flooded to towns such as Belem and Manaus in Northern Brazil
to work in the Amazon Basin. Buildings such as the Amazonas Theater symbolize the
once prosperous Northern Brazil from the “Rubber Boom”. The output of NR from Brazil
was approximately 42,000 tons a year in the late 19th Century, which accounted for
almost the entire global NR market.8 In the early 20th Century, NR production from
British Colonies in Southeast Asia entered the market and devastated the Brazilian NR
economy.9
The success of the Brazilian NR was the envy of the entire world and the British
smuggled H. brasiliensis seeds from Amazon to London in 1876.9 The British scientists developed a higher-yield, more disease resistant variety of H. brasiliensis through grafting and planted them in newly established plantations in the Malaysian Peninsula. 2
The prices of NR from Southeast Asia were significantly cheaper than their Brazilian
counterparts. The main reason for this was because NR produced in Southeast Asia were
planted approximately four meters apart while the NR from Brazil often required the
farmer to walk up to a kilometer between trees.9 The fierce competition between
Brazilian and Southeast Asia NR brought the end of the economic boom of Northern
Brazil.
The Brazilian government did not leave the NR industry without a final attempt to revive Northern Brazil. The Brazilian government partnered with Ford to form Brazil’s
own rubber plantation; over 200,000 trees were planted over 3,200 hectares.7 This
ambitious project was abandoned and posted huge losses with the first reported epidemic
of H. brasiliensis in 1933 by SALB.10 Other attempts to establish a plantation in Brazil or
South America had failed due to the fact that the trees were destroyed before reaching
physiological maturity.
SALB is a rubber tree disease caused by the fungus Microcyclus ulei, an
ascosmycete (sac fungi) that is native to the Amazon area. Modern attempts to control
this disease by chemical (fungicides)11 and biological (breeding and selection)12, 13 methods have failed. As the name implies from SALB, Microcyclus ulei is known to infect young leaves and stems of H. brasiliensis; it was also observed that matured leafs of H. brasiliensis are resistant to M. ulei. In most cases, M. ulei attacks the young leafs of
Hevea, causes grey lesions on the leaf and prevents photosynthesis of these leafs.12 In other words, the development of commercial-scale rubber plantation cannot be realized because the young trees will not be able to mature. Another difficulty in disease control of Hevea is that the resistant genome seems to be a less dominant gene. SALB-resistant 3
plants were crossed with high-yield H. brasiliensis and their offspring are still susceptible to fungal attacks.14
Plant biochemists had been working on fungicides and improved application
techniques over the past few decades. Weekly application of fungicides were attempted
to control the spread of the fungi; however, young plants are difficult to spray without
considerable set-back in growth. Furthermore, Hevea’s wintering cycle involves
secondary leaf fall and refoliation after wintering. Matured Hevea plants are susceptible
to fungal attacks as well. At this time, there are no solution for this problem and led to
large losses of plantations; thus, inhibiting NR production on a commercial scale in
Central and South Americans.7 As Wade Davis commented in his book, "a single act of biological terrorism such as the introduction of fungal spores so small as to be readily concealed in a shoe could wipe out the plantations, shutting down production for at least a decade. It is difficult to think of any other raw material that is as vital and vulnerable."9
In 2005, approximately 21 million tons of rubber was produced and 42% of it (9
million tons) was NR.2, 15 In terms of quantity by type, NR is still the largest. (42% NR,
20% Styrene-butadiene rubber (SBR), 14% latex SBR, 12% polybutadiene, 5% ethylene propylene diene monomer rubber (EPDM), and 7% other synthetics.16) While the USA is
self-sufficient in synthetic rubber production, with substantial export activities, no Hevea
NR is produced in the USA. It is important to emphasize that no synthetic rubber matches
the performance of imported Hevea NR. The development of domestic supply of NR is
recognized in the Critical Agricultural Materials Act of 1984 (Laws 95-592 & 98-284).17,
18 The Act recognizes that NR latex is a commodity of vital importance to the economy
and the defense of the nation. Recently, due to the increased demand of NR from China, 4
Vietnam had doubled its production of NR from 155 thousand tonnes to 320 thousand tonnes in from 1995 to 2001.16 This caused a significant drop in NR market prices. In an attempt to control NR prices, the major NR producing countries (Thailand, Indonesia and
Malaysia) formed an International Tripartite Rubber Council (ITRC) to manage sales and stocks. Since the intervention of the ITRC, NR prices raised from ~20 cents US dollars
(USD) / kg to ~3 USD / kg of NR.
Scientists had been working on NR replacement since World War II (WWII). As a result, new polymers were synthesized and led to the development of SBR, polyvinyl chloride (PVC), chloroprene rubber (CR) and butyl rubber. The growth of synthetic rubbers (SR) was triggered mainly by geo-political events, when NR was in very short supply and high in demand. NR and SR share much of the processing technology; they are first prepared as un-vulcanized compounds and then vulcanized at higher temperature to give the final product.19 In short, the production cycle of both NR and SR is much
longer than thermoplastics due to vulcanization and mixing cycles. In addition, scraps
cannot be easily recycled.19
Despite SR share the same processing technology, their physical properties are not superior to NR particularly in green strength and low hysteresis. Green strength is the tensile strength and/or tensile modulus of an uncured rubber compound. This important processing property relates to the compound’s performance in extrusions, calendaring and tire building, particularly the 2nd stage building machine for radial tires. If tires are
constructed with rubber compounds with poor green strength, they may fail to hold air
during normal expansion in the 2nd stage of tire building prior to cure. While
5 polybutadiene is currently used to construct ~70% of the treads and sidewalls, the use of
NR in tires cannot be replaced or omitted.
In order to resolve these problems, thermoplastic elastomers (TPEs) were developed as a solution to reduce costs of production and processing of rubbers. EPDM blends with polypropylene (PP), thermoplastic polyurethanes, and polystyrene block copolymers blended with PP are a few examples of TPEs.20 Even though many new materials are introduced as NR replacement, the shift to thermoplastic technologies does not impact the NR industry to a great extent. Despite the cost efficiency, the thermoplastic replacement counterparts still do not always perform as well as NR in many ways.
This thesis will investigate NR biosynthesis to get a better understanding how the tree produces NR. Insight into the biosynthesis may lead to the development of a biomimetic system that would produce NR.
6
CHAPTER II
BACKGROUND
2.1. Chemical Structure of Natural Rubber
From the pyrolysis of NR, scientists realized that NR can be broken down to isoprene (IP). NR is stable below 200 oC and significant decomposition into smaller
fragments takes place beginning at 290-300 oC.21, 22 The main pyrolysis product of NR is
DL-limonene when pyrolysis is carried out below 450 oC (Figure 2.1.1a) and IP when further pyrolysis (retro Diels-Alder reaction) is performed (Figure 2.1.1b).21
b) a)
isoprene DL-limonene
Figure 2.1.1 - DL-limonene (a) and isoprene (b).
From this understanding, Bouchardat reported the first polyisoprene (PIP)
synthesis in 1879 using IP as the monomer and hydrochloric acid as the initiator.23-25 This
report quickly triggered research interests; however, the subsequent work was slow and not fully successful because high molecular weights were not reached and the mechanical
properties of the cured PIP were poor.24, 26 7
The how and why of rubber formation in Hevea trees are long-standing mysteries.
It was the analysis of Hevea rubber that led to the acknowledgement of the existence of macromolecules where the monomer units are connected by covalent bonds. Samuel
Shrowder Pickles of the Royal Institute of London was the first to propose a chain structure based on the building block27, 28 as shown in Figure 2.1.2a. Prior to 1910, NR
was believed to have a structure based on the self-assembly of dimers (Figure 2.1.2b)
held together by physical forces.28 Carl Harries based this proposal on the fact that he
found no end groups in natural rubber. Chemists at the time did not want to accept the existence of macromolecules.19, 29
Figure 2.1.2 - Suggested building blocks of NR before (b) and after (a) 1910.27
Infrared and nuclear magnetic resonance (NMR) spectroscopy, and X-ray studies
have shown that the major component of NR from Hevea brasiliensis is polyisoprene
(PIP) in cis-1,4 configuration, with about 6 wt% non-rubber components (mostly
proteins).30-33 The general agreement from the literature is that Hevea NR contains a
dimethyl-allyl head group followed by 2 units in trans-1,4 configuration from the
initiator, followed by >5000 cis-only units (Figure 2.1.3).33-35 Hevea NR has very broad
8
36, 37 molecular weight distribution (Mw/Mn ~ 2-15). Biochemical studies provide no information on the termination step of rubber formation; a variety of end groups
(hydroxyl, aldehyde, and amine, etc) have been found.23, 28, 29
Figure 2.1.3 - Chemical structure of NR.3 Head (α) and end group (ω) structure is not proven.
High molecular weight (MW) NR produced by other plant species such as
Parthenium argentatum (Guayule) and Ficus elastica have similar structures.34, 38, 39 13 C and 1H NMR spectroscopy are powerful tools for structural analysis of polymers; however, the exact structure of NR remains unproven due to its very high MW.33, 35
Figure 2.1.4 shows the 13C NMR spectra of PIPs isolated from Hevea and Guayule.33, 40
The signal at 32.3 ppm is assigned to carbon A (-CH2-C(CH3)=), and the signal at 26.4
ppm is assigned to carbon D (=CH-CH2-). The peak at 23.3 ppm is assigned to the carbon
of the methyl group (CH3-C(CH2)=) attached to carbon B. The signals at 135.1 and
125.1ppm are assigned to the olefin carbons B (=C(CH3)(CH2)-) and C (=CH-CH2-).
9
Figure 2.1.4 - 13C NMR spectra of NR from Hevea40 (a) and Guayule33 (b).
As mentioned before, the head and end group structures remain unproven. Tanaka analyzed naturally occurring lower MW (Mn ~ 20,000 g/mol) NR from a mushroom
(Lactarius volemus).33, 41 Figure 2.1.4 shows the 13C NMR spectrum with our assignments. The signal at 32 ppm is assigned to carbon A (-CH2-C(CH3)=), and the
signal at 27 ppm is assigned to carbon D (=CH-CH2-) in the main chain. The peak at 22
ppm is assigned to the methyl group carbon E (CH3-C(CH2)=) attached to carbon B. The
signals at 138 and 123 ppm are assigned to the olefin carbons B (=C(CH3)(CH2)-) and C
(=CH-CH2-). Tanaka assigned the signal at 18 ppm to the methyl carbons of the dimethyl
allyl head group (Fα), and the signals at 130 ppm to the olefin carbon Bα,tr1 of the trans
41 head group. The peak at 40 ppm was assigned to carbons Aα,tr1 and Aα,tr2 of the methylene groups of the two trans units attached to the dimethyl allyl head group (-CH2-
C(CH3)=). The methyl protons in the first two trans α-units (note that Tanaka labeled the head group as ω, so we changed the notation on the original NMR spectrum according to
polymer chemistry principles) were labeled as Eα,tr1 and Eα,tr2 and appear around 16 ppm.
As for the ω-end group, Tanaka assigned signals at 142 and 120 ppm to the olefin 10
’ carbons Bω (=C(CH3)(CH2)-) and Cω (=CH-CH2-) respectively. He also suggested the
41 peak at 60 ppm to be the methylene carbon next to an l ester end group (Gω). The carbonyl carbon (H) appears at 176 ppm, and signals I, J, K and L were assigned to the fatty acid residue of the ester end group. The suggested structure of Hevea NR is based on this work.
Figure 2.1.5 - 13C NMR spectrum of NR from L. volemus.33, 41 11
It is well-established that NR is composed of long-chain branched molecules.42-44
Fulton et al. showed the presence of long-chain branching and gel in Hevea NR by Field
Flow Fractionation (FFF): the log Rg – log MW conformational plot was shown to have a slope of 0.3 in the high MW range.45 Hevea NR contains 50–70% gel. Tanaka established that the gel has two different components that he termed “hard” and “soft” gel. The soft gel is produced by hydrogen bonding between phosphates and phospholipids at the ω-end group of Hevea NR. It has been shown that the addition of 1–2% ethanol into a Hevea
NR solution in a good solvent, such as toluene, dramatically decreases the gel content by breaking the hydrogen bonds that make up the “soft” gel, as shown in Figure 2.1.5.33, 37
Figure 2.1.6 - Deproteinization by treatment with 1~2% ethanol.37 (DMAPP denotes dimethylallyl pyrophosphate, FPP denotes Farnesyl pyrophosphate.)
12
The “hard gel” crosslinking points are believed to be formed by radical reaction between sulfur containing proteins and the dimethyl allyl double bond in the α-head groups of NR. These covalent bonds can be broken via transesterification.46
The exact structure of high MW NR remains to be proven by the next generation of scientists.
2.2.History of Natural Rubber
NR has a long and distinguished history. Ancient Mesoamerican peoples mixed the rubber latex harvested from the Castilla elastica shrub with the juice of Ipomoea alba
(a species of the morning glory vine) and produced solid rubber. Rubber balls made by the Olmec of Mesoamerica (often referred to as the “rubber people”) dated back to 1600-
1200 B.C.1 Mexican excavations found rubber balls dated 600 A.D. that were used in religious ceremonies and ball games. In 1403, Columbus reported that the natives of Haiti played games with balls prepared from the gum of a tree. In 1520, Fernando Cortes, a
Spanish “conquistador” observed rubber balls in games played at the Inca king
Montezuma’s palace.47 In 1735, Condamine, French explorer, brought a sample of rubber from Peru to France, made from the latex called “cahuchu” (milk of the tree) by natives.
He spelled the word as “caoutchouc” in French, which was later spelled as “kautschuk” in German.48 In 1752, Priestly coined the word “rubber”, referring to the ability of the material to “rub out pencil marks”.47 In 1820, McIntosh made a raincoat from cloth impregnated with NR. The coat was water repellent - in Great Britain the word
“McIntosh” is still synonymous with “raincoat” - but it was smelly and sticky.49 The
13
stickiness of rubber arises from free polymer chains moving independently. Hancock
perfected the process by “curing” or crosslinking the rubber using sulfur which made it
lose its stickiness because these free chains are now chemically bonded. As mentioned before and according to legend, Charles Goodyear accidentally dropped NR mixed with sulfur and white lead on a hot stovetop in 1839. This process cured NR fast enough to become the foundation of rubber technology.1 Akron, Ohio became the “rubber city”
when Seiberling and Miles built their first tire manufacturing plant and named it after
Goodyear. Buchtel College (today the University of Akron) offered the first course in
rubber chemistry in 1914.
World War II (WWII) threatened the access of the Allied Forces to the sources of
NR, by then mostly in Southeast Asia, because a pathogenic attack wiped out the
plantations in Brazil. Every tire, hose, seal, and valve, which were essential to war craft
required rubber. The “Synthetic Rubber Procurement Program” headquartered in Akron
was second in order of importance only to the “Manhattan Project” to make the atomic
bomb.50 The ultimate goal of the rubber program was to establish a domestic source of
rubber. This surge of research and commercialization effort led to the production of a
wide range of synthetic rubbers SR. In addition to the focus of trying to synthesize a NR
replacement, the program explored alternative plants to produce NR, including planting
Russian Dandelions in 41 states.51, 52 By 1964, SR made up 75% of the market53;
however, the ultimate goal of completely replacing NR with a synthetic alternative was
not accomplished.
The re-emergence of NR research was marked by the OPEC oil embargo of 1973,
which nearly doubled the price of SR. In addition, an unexpected threat was brought to
14 the synthetic market by the rapid adoption of the radial tire. The construction of radial tires necessitates the use of NR that possesses the required physical properties. By 1993, natural rubber had recaptured 39% of the domestic market.53 Today we still do not have a synthetic replacement.
In the next Chapter we will briefly review the history of efforts to produce an NR equivalent synthetically.
2.2.1. Synthetic Polyisoprenes
It has long been a fascination of chemists to create a chemical and physical equivalent of NR. Various catalytic systems have been investigated.54-57 Table 2.2.1 summarizes the microstructures of synthetic polyisoprenes (PIPs) obtained by various polymerization techniques. The possible microstructures of PIP are shown in Figure
2.2.1. It can be seen that no methods produced fully cis-1,4 PIP enchainment.
Table 2.2.1 - Microstructures in synthetic PIPs
15
Figure 2.2.1 – PIP microstructures. *an example of C15 is shown, other cyclics may occur.
The cationic polymerization of IP was studied first by Gaylord et al. in 1966.26 It was found that AlEtCl2 or SnCl4 in n-heptane yielded low conversion (~20%) and the resulting PIP mostly consisted of trans-1,4 chain enchainment with a few repeat units
26 with cis-configuration. TiCl4 in n-heptane was found to be inactive unless hydrous n- heptane was added. The rates of polymerization in aromatic solvents were generally much higher due to extensive chain transfer to solvent. The stereo-regularity of the resulting polymers was found to be mostly trans-1,4 with Mns around ~50,000-100,000
58 g/mol and Mw/Mn ~8 due to cyclic side products. In halogenated solvents, the rate of polymerization was reported to be the fastest among the three types of solvents discussed.
In solvents of higher polarity, such as o-dichlorobenzene, more linear structures were obtained. The resulting polymers contained higher cis-content (~30%).58 In a more recent study in 2008, Khachaturov et al. initiated cationic polymerization of IP by a TiCl4- trichloroacetic acid system in dichloromethane.59 They reported ~50% cyclized product and ~50% loss of unsaturation due to cyclization. Of the remaining unsaturation ~47% was found to be trans-1,4, with ~1.5% cis-1,4 and ~1.5% 3,4.60
16
The radical polymerization of IP was also investigated in 1960s. Gobran et al.
studied the bulk polymerization of IP using 2-azo-bisisobutyronitrile (ABIN) and benzoyl
o 61 peroxide as initiators at 60~90 C. The authors obtained low MW PIPs (Mn =
1,000~7,000 g/mol) and determined that the radical polymerization of IP was a dead-end polymerization. Dead-end polymerization is a term coined in the 1950s by Tobolsky
describing a polymerization that can only reach a limiting conversion due to initiator
depletion.62 In the 1990s, Solomon, Moad and Rizzardo showed the first examples of nitroxide-mediated free radical polymerization (NMP) of vinyl monomers.63 Hawker et al. attempted the NMP (Nitroxide Mediated Radical Polymerization) of IP using 2,2,5- trimethyl-4-phenyl-3-azahexane-3oxy-nitroxide.64 (Figure 2.2.2) In 36 hours, they
64 achieved 75% conversion with Mn = 19,800 g/mol and Mw/Mn = 1.07.
Figure 2.2.2 – NMP of IP using 2,2,5-trimethyl-4-phenyl-3-azahexane-3oxy-nitroxide as initiator.64
The authors did not explore the microstructure of the resulting polymer. In 2006,
Perrier et al. attempted controlled radical polymerization of IP via reversible addition- fragmentation chain transfer (RAFT).65 The authors used two different RAFT agents: 1)
2-(2-cyano-propyl)dithiobenzoate and 2) 2-ethylsulfanylthiocarbonyl-sulfanylpropionic
65 acid ethyl ester (ETSPE). They were able to achieve 97.2% conversion, Mn = 27,400 g/mol, and Mw/Mn = 1.47 in 72 hours using the ETSPE RAFT agent. The resulting 17
polymers had 75% 1,4-, 20% 3,4-and 5% 1,2-addition.65 Atom transfer radical
polymerization (ATRP) of IP have not been realized because dienes chelate to the copper
catalyst.65
The anionic homopolymerization of IP was researched extensively in the 1950s
and 1960s. Tobolsky et al. did a systematic study of IP polymerization with various
solvent systems.66, 67 The authors were able to obtain 94% cis-1,4 polyisoprene initiated
66 with n-butyllithium in n-heptane with Mυ = 2,000~150,000 g/mol. They concluded that
high cis-content can be obtained by using hydrocarbons as the solvent.67 Morton et al.
studied the effect of addition of tetrahydrofuran (THF) into the anionic polymerization of
IP in 1963.68 The authors found that 3,4-enchainment increased dramatically.68, 69
Bywater et al. continued this study using cyclohexane/THF solvent systems and found that the polarity of the solvent affected the effective counter cation size.70 The recent
literature on anionic polymerization of IP has focused on block copolymer synthesis.71-73
Ziegler-Natta and metallocene catalysts yielded the highest cis content in IP polymerizations. More recently research focused on Nd-based catalysts activated by R3Al that display high cis-1,4 stereo-specificity in both the homo- and copolymerization of
IP.74 However, early versions of these catalysts were limited by the lack of control over
56 MWs and Mw/Mns. It was hypothesized that this problem was attributable to the
heterogeneity of the catalyst systems and the multiple active species.56 In 2003, Dong et
al. circumvented these problems by introducing a [Nd(O-iPr)3]/modified
methylaluminoxane (MAO) catalyst system.75 The improved solubility of MAO in
heptane allowed for a homogeneous single active site system. The authors have tried
various reaction conditions for this system. In heptanes an [Al]:[Nd] ratio of 100:1 at 30
18
4 °C gave 98.9% conversion with Mn ~5x10 g/mol, Mw/Mn = 1.14 and 91.4% cis-1,4
structure.75 In toluene, an [Al]:[Nd] ratio of 300:1 at 30 °C gave 100% conversion with
4 75 91.7% cis-1,4 structure with Mn ~8x10 g/mol and Mw/Mn = 2.21. In dichloromethane,
the authors obtained mainly cyclized trans-1,4 structures. In their 2005 follow-up study
of Nd-based metallocene, Taniguchi and Dong et al. reported a ternary catalyst system
composed of Nd(III) isopropoxide, dimethylphenylammonium
tetrakis(pentafluorophenyl)borate, and triisobutylaluminum.56 They found the optimal
catalyst composition to be a [Nd]:[borate]:[Al] = 1:1:30, which gave greater than 97%
conversion, Mn = 200,000 g/mol, Mw/Mn of 2.0, and approximately ~90% cis-1,4
structure.56 Unfortunately these systems yielded much lower MWs than that found in
Hevea NR. The closest commercial attempt to mimic NR was accomplished by the
Goodyear Tire&Rubber Company with their product called Natsyn® produced with a
5 titanium-aluminum (Ziegler-Natta type) catalyst with Mn = ~2x10 g/mol, Mw/Mn of ~3 and ~98.5% cis content. 55
It is our belief that in order to be able to create SR that mimics the structure and
properties of NR, we need to understand NR biosynthesis. The following sections
summarize our understanding of in vivo and in vitro NR biosynthesis from the viewpoint
of polymer chemistry.
2.3. Natural Rubber Biosynthesis
2.3.1. Rubber Producing Plants
NR is obtained from latex, an aqueous emulsion present in the laticiferous vessels
(ducts) or parenchymal (single) cells of rubber-producing plants (Figure 2.3.1). Although
19
more than 2,500 plant species are known to produce NR, there is only one important commercial source, Hevea brasiliensis (the Brazilian rubber tree). The rubber
from Guayule, Parthenium argentatum, is being developed as a non-allergenic NR
mainly for rubber gloves.76, 77
The rubber latex from H. brasiliensis is harvested by “tapping” the rubber tree.
An incision is made on the trunk and latex will ooze out of the incision. This white liquid
is collected and then coagulated to yield high molecular weight (Mn >1 million g/mol) polymer. Guayule, Parthenium argentatum, is grown in the Southwestern USA. Guayule latex is mainly used for advanced medical and consumer products. The guayule rubber is produced by a green aqueous-based extraction process on a commercial scale.78 Russian dandelion, Taraxacum kok-saghyz, is being developed as a rubber-producing crop in the
Northern USA.38, 79 Figure 2.3.1 shows an array or rubber producing plants that have
been of research and commercial interest. Hevea is the most studied NR, so Hevea will
be discussed in more detail.
Figure 2.3.1 - Examples of rubber producing plants.
20
2.3.2 Anatomy of the Hevea NR Latex
The productivity of Hevea trees is usually as high as 50–100 g latex per day in a mature tree.80 Depending on the seasonal effects and the state of the soil, the average
composition of Hevea latex is 25~35 wt% cis-1,4-polyisoprene (PIP), 1~1.8 wt% protein;
1~2 wt% carbohydrates; 0.4~1.1 wt% lipids, 0.5~0.8 wt% amino acids, and 50~70 wt%
water.81 The rubber particles have a distribution of diameters ranging from 0.1 to 10 μm33
(Figure 2.3.2a) and are stabilized in the cytosol by a membrane of phospholipid monolayer (Figure 2.3.2b).4 The cytosol contains mainly water, salts, organic molecules and ribosomes.82 The cis-prenyltransferase enzyme (Figure 2.3.2b) is a membrane-bound amphiphilic enzyme found in NR producing plants, yet to be isolated and fully characterized.33, 83
Figure 2.3.2 - Visualization of NR particles and its structure.18
It has been known since the 1950s that the “chain elongation” of rubber molecules proceeds by the addition of the isopentenyl pyrophosphate (IPP) monomer.84, 85 The initiator is believed to be farnesyl pyrophosphate (FPP).86 These molecules are water-
21 soluble and are present within the cytosol along with the divalent metal “cofactors”
(Figure 2.3.2b), needed to be present in the biosynthesis process that will be discussed in
the next section. The biosynthesis of NR is catalyzed by the rubber transferase enzyme, cis-prenyl transferase.4, 84, 87, 88 Enzymes are proteins that act as highly selective catalysts
in biochemical reactions. The rubber transferase is integrated into the phospholipid
monolayer that surrounds the latex particles. The phospholipid monolayer stabilizes the
particles to prevent aggregation in the aqueous medium. The hydrophobic polymer chains
reside within the latex particles, and polymerization proceeds at the active sites of the
enzyme.34 The rubber transferase enzyme, which has not been isolated yet, is proposed
to be amphiphilic, with hydrophilic regions facing the cytosol to allow the access of
hydrophilic building blocks and the hydrophobic regions accommodating the growth of
NR.
2.3.3 Biochemical Pathway of Natural Rubber Biosynthesis In Vivo
As mentioned before, it is accepted in the literature that the monomer to make NR
is IPP. Figure 2.3.3 shows the structure of IPP, which can be considered to be an adduct
of pyrophosphoric acid (H4P2O7) and isoprene (IP).
Figure 2.3.3 - Structure of isopentenyl pyrophosphate IPP at pH = 7.4.89
22
At the physiological pH of 7.4, IPP is a stable di-anion with two potassium
counter cations. The cytosol has a high concentration of potassium ions (139 mM) and low concentration of sodium ions (12 mM) for osmoregulation purposes.82 In contrast, in
the human blood, the potassium concentration is only 4 mM and the sodium
concentration is145 mM.90
IPP is produced from carbohydrates in plants, bacteria, algae, and mammals,
including humans. The synthesis of IPP can proceed by two different pathways: the
mevalonate (MVA) pathway and non-mevalonate (non-MVA) or deoxy-xylulose
pathway. These two distinct pathways have evolved in different organisms. In eukaryotes
(cells that contain nuclei that carry genetic information), IPP is derived from acetyl-CoA
(coenzyme A), while in prokaryotes (cells that lack nuclei) and plant chloroplasts, IPP is
derived from 1-deoxy-D-xylulose-5-phosphate.91 In higher plants, the mevalonate pathway operates mainly in the cytoplasm and mitochondria, whereas the non-MVA
pathway operates in the plastids.92 Plastids are sub-units in a plant cell that are
responsible for photosynthesis; they also serve as storage units for fatty acids and terpenes found in plants. It is suspected that the IPP for NR biosynthesis is derived from the MVA pathway located in the cytosol.93 However, IPP produced by the 1-deoxy-D-
xylulose-5-phosphate pathway may also diffuse from the plastids to the cytosol.94
The biosynthesis of polyisoprenoids or terpenoids is believed to be regulated by a series of chemical equilibria shown in Figure 2.3.4. IPP is first isomerized into dimethyl allyl pyrophosphate (DMAPP) by the isomerase enzyme. DMAPP may serve as the initiator for subsequent terpenoid synthesis (chain growth or polymerization) catalyzed by appropriate enzymes. Longer chain initiators (Figure 2.3.5) are synthesized by trans-
23 prenyltransferases. When excess IPP is present, the equilibrium shifts toward DMAPP which in turn can be converted into isoprene (IP) by the isoprene synthase enzyme.Because of its low boiling point (34oC) IP easily evaporates, so the corresponding equilibrium is shifted towards IP to remove excess IPP. The estimated rate of IP production by the human body is 0.15 µmol/kg/h, which corresponds to about 17 mg each day for a 70 kg person. Vegetation emits 600 megatons of IP per year into the atmosphere – major producers are oak trees, tropical broad leaf trees and shrubs. Figure
2.3.4 presents our rendition of the IP biocycle.
Figure 2.3.4 - Terpenoids biosynthesis cycle.
The C15 farnesyl pyrophosphate (FPP) shown in Figure 2.3.5 is believed to be the initiator in the in vivo biosynthesis of Hevea rubber based on numerous reports of α-trans
head groups found in 13C NMR spectrum of low MW rubbers, but it is not proven for
Hevea.33
24
For better chemical understanding of the compounds, we will use –OPP to denote pyrophosphate groups. In the biological literature, the pyrophosphate group is typically written as –PPi. In the presence of the metal cofactors (Mg2+ or Mn2+ in vivo and Mg2+ in vitro) and the rubber transferase enzyme, an IPP unit adds to extend the FPP by one more unit but in cis configuration. Each step is accompanied by the liberation of pyrophosphoric acid. This step is repeated and the process generates NR with more than
5000 units. (Figure 2.3.5).
+ OPP OPP
Farnesyl pyrophosphate Isopentenyl pyrophosphate
cis-prenyltransferase metal2+ cofactor
OPP HOPP 2
cis-prenyltransferase metal2+ cofactor
OPP 2 >5000
HOPP
Figure 2.3.5 - Synthesis of NR in H. brasiliensis. OPP stands for the pyrophosphate end- group and HOPP represents pyrophosphoric acid.
The FPP initiator has successfully been used to make Hevea rubber in a culture tube (in vitro biosynthesis, to be discussed later). Other oligomeric allylic pyrophosphates
(geranyl-, farnesyl- and geranyl-geranyl-pyrophosphate) can also serve as initiators in vitro. The chemical structures are shown in Figure 2.3.6.
25
Figure 2.3.6 - Structure of the allylic oligoisoprene pyrophosphates. DMAPP: dimethyl allyl pyrophosphate, GPP: geranyl pyrophosphate, FPP: farnesyl pyrophosphate, GGPP: geranylgeranyl pyrophosphate.
Our rendering of the initiation and propagation steps are shown in Figure 2.3.7 using symbolism from biochemistry. When compared with the polymer chemistry symbolism shown in Figure 2.3.5, both show the stepwise addition of the building blocks, with the elimination of a pyrophosphoric acid in each step. The monomer (IPP) is termed
“substrate” while the initiators are termed “cosubstrate” in the biochemical literature.
26
Figure 2.3.7 - Biochemical representation of rubber biosynthesis.34
As mentioned before, enzymatic activity requires the presence of divalent cations such as Mg2+ or Mn2+ in vivo , called “activity cofactors”.4 The exact role of the cofactors is still unclear. Termination is believed to occur when the chain end detaches from the enzyme. During this step the –PP terminus may hydrolyze, yielding an -OH end group as shown in Figure 2.1.3. This end group may react with fatty acids, yielding ester end groups shown in Figure 2.1.4.
27
2.3.4 Prenyltransferases
Prenyltransferases are enzymes that catalyze the synthesis of various isoprenoid compounds: sterols, terpenes, and natural rubber. Based on the configuration of the repeat
units in the products, prenyltansferases are classified into two classes: trans- and cis- prenyltransferases. In both prokaryotes and eukaryotes, trans-prenyltransferases catalyze the formation of geranyl diphosphate (GPP:C10), farnesyl diphosphate (FPP:C15), and geranylgeranyl diphosphate (GGPP:C20) (Figure 2.3.6) These compounds then serve as initiating species to produce many other longer chain isoprenoids necessary for cellular growth and survival. Figure 2.3.8 shows the structure of an avian trans-prenyltransferase that catalyses FPP synthesis from DMAPP and IPP. The binding sites for the DMAPP and IPP were located within the hydrophilic regions of the enzyme (red arrows), whereas chain growth was proposed to take place within a hydrophobic pocket positioned toward the bottom end of the conical enzyme (Figure 2.3.8).
Figure 2.3.8 - A scheme of the active sites in an avian trans-prenyltransferase.95 The oval represents a large motive proposed to stop chain growth.
28
Mutational analyses and x-ray crystallographic investigations revealed crucial amino acid residues in the conserved domains of various trans-prenyltransferases to stop
the chain growth, accounting for the mechanism of chain length determination.95-97 The
structural genes for FPP synthase98-100 and GGPP synthase101-103 have been cloned and
characterized from various organisms. However, only three cis-prenyltransferase genes
have recently been cloned104, 105 from E. coli, M. luteus and yeast, which share a low level of sequence homology (~30%). The genetic sequences of the rubber transferase remain unidentified because it is a membrane-bound enzyme in low abundance.4 The fact that the enzyme activity is rapidly lost upon disruption of the structural integrity of the membrane poses one of the great challenges in sequencing the enzyme.87, 106 Generally, rubber
transferase is accepted as an amphiphilic enzyme residing at the interface of the latex
(Figure 2.3.8). Propagation occurs when the initiator or the NR molecule is bound at the specific catalytic site within the funnel-like crevice of the enzyme and is activated by co-
factors, and IPP enters from the aqueous phase.
2.3.5 Mechanism of Prenylation in Short Chain Isoprenoids
The mechanism of short-chain terpenoid biosynthesis proposed and proven by
Poulter86 is illustrated in Figure 2.3.9. According to the authors, resonance stabilized allylic carbocations are generated by the dissociation of the –OPP end group. Then the allylic carbocation reacts with the double bond of the IPP, and a pyrophosphoric acid,
HOPP, is released. The dissociative mechanism (SN1) was proven by constructing the
Hammet plot for prenyl transfers with fluorine substituted allylic pyrophosphates.
29
OPP prenyltransferase OPP
OPP OPP
OPP OPP
HOPP H OPP
Figure 2.3.9 - The mechanism of terpenoid biosynthesis proven by Poulter et al.86
The polymer chemistry community has been reluctant to accept this mechanism,
although ionic polymerizations in aqueous media have been demonstrated.107
2.3.6 Proposed Mechanism of Natural Rubber Biosynthesis: Natural Living
Carbocationic Polymerization (NLCP)
Based on Poulter’s work, Puskas et al. proposed that NR biosynthesis most likely
also proceeds by a carbocationic mechanism (Figure 2.3.10).35 According to this
proposal, the initiation starts with an enzyme (and divalent cofactor) – assisted ionization
of the carbon-oxygen bond of the initiator and yields an allylic carbocation plus a
pyrophosphate counter-anion; the enzyme plus cofactor(s) coordinate with the pyrophosphate “protecting” group and mediate the formation of the initiating
carbocation. According to polymer chemical convention, the enzyme plus cofactors
30
constitute the co-initiating system. Ionization at the chain end is favored by resonance
stabilization of the allylic carbocation and increasing entropy of the system.
Subsequently, IPP adds to the allylic carbocation, yielding a tertiary carbocation which,
via proton elimination, regenerates the trisubstituted allylic pyrophosphate.35 This
mechanism applies to the formation of trans-1,1-dimethylallylic initiators (natural initiators invariably are trans), catalyzed by trans-prenyl transferase, as well as to the incorporation of the subsequent cis-units catalyzed by cis-prenyl transferase. In regards to trans or cis-stereoregulation, Puskas proposed that the specific enzyme functions as the template. The template theory was originally proposed by McMullen108. He suggested
that polynucleotides complex with the rubber and act as template. However, it has been
demonstrated that polynucleotides are not involved in NR biosysthesis. The incorporation
of each IPP unit is always accompanied by the loss of pyrophosphoric acid HOPP (or its
salts).
Figure 2.3.10 - Proposed NLCP mechanism of NR biosynthesis.35 31
This mechanism is very similar to Yokozawa et al.’s109-111 general mechanism for the biosynthesis of many natural biopolymers. These authors developed the concept of
“chain-growth polycondensation”, according to which an enzyme activates the initiating entity and/or the dormant polymer chain end, which proceeds to add monomer and the enzyme complex relinquishes the protective end group to regenerate the chain end.
Figure 2.3.11 helps to visualize Yokozawa’s concept. As opposed to synthetic polycondensation, the monomer is inactive and can only react with the activated initiator or polymer chain end.
Figure 2.3.11 - Yokozawa’s concept of chain-growth polycondensation.109, 110
Examples cited by these authors include peptide extension (termed “elongation”
in biochemistry), DNA and RNA syntheses and natural rubber biosynthesis.109-111
Yokozawa’s group developed two strategies for chain-growth polycondensation. The first
32 strategy involved the activation of polymer end groups, and led to aromatic polyamides, polyesters, polyethers, poly(ether sulfone) and polythiophene.110 By the second strategy, the monomer was separated from the polymerization phase to prevent monomer- monomer and polymer-polymer condensations. Yokozawa’s work was a breakthrough in biomimetic polymer synthesis and produced living polycondensation reactions displaying narrow MWDs. The synthesis of cis-PIP was attempted as shown in Figure 2.3.12. The electrophilic initiator (triphenylmethyl (trityl) perchlorate) was postulated to create an allylic end group structure. This structure was expected to be reactive with the unreactive monomer structure, accompanied by the elimination of the protecting allyl trimethyl silane group. However, only elimination happened and a diene was obtained.110
Figure 2.3.12 - Attempted “bio-inspired” synthesis of cis*-1,4-polyisoprene.110 *(The resulting polymer was in the trans conformation)
The proposed chain-growth polycondensation mechanism should lead to monodisperse PIP; however, all natural rubbers exhibit multimodal/broad molecular weight distributions. This most likely is due to continuous initiation with simultaneous
33
chain growth. It should be noted that all industrial rubbers exhibit broad MWD which is
required for better processing and the required balance of properties.
2.4 In Vitro Natural Rubber Biosynthesis
The first in vitro polymerization system was described by Archer et al. in the
1980s. They incubated 14C-IPP in the presence of unlabeled neryl pyrophosphate (NPP)
or geranyl pyrophosphate (GPP) initiators in a suspension of Washed Rubber Particles
(WRP) isolated from living Hevea latex, and showed the incorporation of the
radiolabeled IPP.84 The presently accepted method to determine the activity of rubber
transferases is based on this work: the activity is calculated based on the incorporation
rate of 14C IPP monomer into existing chains or forming new chains from the initiator in
vitro.87, 112, 113 This is accomplished by establishing a double reciprocal plot of kinetic
data (a.k.a. Lineweaver-Burk plot) with 14C-IPP. The isolated WRPs are incubated with a
predetermined amount of APP (Allylic Pyrophosphate) initiator and 14C-IPP (substrate)
for 60 minutes. The unreacted 14C-IPP monomers were extracted from the rubber and the
radioactivity was measured by scintillation spectrometry (SS). In enzyme kinetics,
biochemists report the enzymatic activity by reporting the Michaelis-Menten (binding)
114, 115 constant (KM) of an enzyme. To determine this value, biochemists flood the enzyme
with substrates to a limiting condition where all the active sites are bound with substrates
and reach a theoretical maximum reaction velocity (VMax). At this point, the reaction rate
of the enzyme is limited to the intrinsic turnover rate of the active site. The inverse of the
reaction velocity data is plotted against substrate concentration to determine the
34
Michaelis-Menten constant (KM), which can be found from the x-axis intercept of the
114, 115 Lineweaver-Burk plot. (Figure 2.4.1). The slope of the plot is KM/Vmax.
Figure 2.4.1 – Lineweaver-Burk Plot of inverse reaction velocity (V) vs IPP concentration in the determination of the enzymatic activity of Guayule WRP.116
By comparing the KM between WRPs from various plant species or even within batches of WRPs from the same plant, the enzyme activity of WRPs can be established. It was found that the rate of rubber biosynthesis in vitro increases with the size of allylic diphosphate initiator, and that initiation regulates the overall rate of rubber biosynthesis.
Therefore, FPP and longer isoprenoids are utilized as synthetic initiators for in vitro NR
biosynthesis systems.
Tanaka’s group established a new method for in vitro rubber biosynthesis using the fresh bottom fraction (BF) of NR latex.117, 118 After filtering out particles and coagulated rubber using a muslin cloth, the liquid latex was centrifuged. After centrifuging three phases were observed: an upper phase, a middle clear phase called C- serum (CS) and a bottom phase (BF).117 Instead of using the WRPs (top layer), the
35 authors used BF for in vitro NR biosynthesis as they believed that the BF contained all the necessary components for NR biosynthesis in comparison to the WRP. Using gravimetric analysis they observed that more than ~10 wt% new rubber was formed with the addition of 14C labeled IPP or FPP to fresh BF.118 The formation of new rubber was confirmed by the incorporation of 14C radioactive IPP into the resulting rubber.118 Figure
2.4.2 compares the UV traces of the endogenous NR from BF and the in vitro NR rubber.
The BF has a high molecular weight fraction around ~106 g/mol with a lower MW tail.
Newly-formed rubber produced a peak at about ~105 g/mol. The radioactive traces also revealed that while the 14C-IPP incorporated into new chains, it also added to pre- existing chains in the lower MW tail fraction of the BF.118
Figure 2.4.2 - SEC trace of Hevea BF (dashed line) and in vitro NR (solid line) .118
It was also found that a small amount of new rubber formed in active BF without the addition of IPP and FPP, concluding that BF contains all of the enzymes and precursors necessary to produce rubber.119 Wititsuwannakul’s group in Thailand also 36
developed their unique Washed Bottom-fraction Particles (WBP)s for in vitro NR
biosynthesis.83 WBPs contains BF and non-rubber particulates such as lutoids
(membrane-bound bodies that cause flocculation of rubber particles) and Frey-Wyssling complexes (globules associated with plant metabolism).83, 120 It was observed that WBPs
are able to incorporate radioactive IPP into NR and the activity is enhanced in the
presence of sodium dodecyl sulfate detergent.120 This is most likely due to the fact that
detergents aid latex stabilization. More recently, Wititsuwannakul’s group investigated
the addition of two cloned suspected gene sequences of Hevea rubber transferase
expressed in E. Coli.83 It was found that a combination of one of the cloned Hevea rubber
transferase sequences with WBP promoted NR growth. In addition, the cloned Hevea
rubber transferase sequence by itself was able to synthesize polyisoprenoids chains in the
104 g/mol range.83
Benedict et al. investigated the in vitro synthesis of guayule rubber using WRP,
synthetic IPP monomer and DMAPP initiator.113 Their WRP was prepared from stems of
P. argentatum, after removal of the bark and impurities. The rubber latex was centrifuged and the top rubber particulate layer was collected and purified as the WRP. The authors used a SEC coupled with a scintillation spectrometer to demonstrate that radioactive IPP incorporated into NR.113 They observed that rubber was formed with a peak at ~105 g/mol within 15 minutes, and that the rubber was able to grow to ~106 g/mol in 180 minutes
(Figure 2.4.3).113
37
Figure 2.4.3 - in vitro guayule NR biosynthesis.113
Cornish et al. developed a method to produce WRPs that will be utilized in our studies. This method is an improvement of Benedict’s group’s WRPs preparation method, where the top rubber particles are collected and purified by repeated buffer washes and centrifugation.87 Her group determined the MW of in vitro NR by means of dual-labeled liquid SS.121 By introducing both radioactive IPP monomer and FPP initiator
into in vitro NR biosynthesis, an average MW of newly formed rubber could be calculated from a ratio between the 14C-labeled monomer and the 3H-labeled initiator.121,
122 The authors assumed that one initiator molecule is used to initiate one rubber chain,
and the IPP monomer is not consumed by the extension of pre-existing chains. Then, the
MW can be calculated as: [((14C-IPP incorporation rate) + 3(3H-FPP incorporation rate)) x MW of IP / [3H-FPP incorporation rate + diphosphate MW], which represents a
monomer / initiator ratio to obtain MW. The three in the formula represents the 3
isoprene units of FPP.121 This method works well in the 104-105 Da range. Outside of this range, the radioactivity of the initiator becomes very low and leads to experimental error. 38
Cornish et al. demonstrated that increasing the amount of IPP while keeping the FPP
concentration constant resulted in increased MW in three different types of WRPs
(Figure 2.4.4).121, 122 Cornish et al. published MW values which were lower than those found by Tanaka’s and Wititsuwannakul’s group where MWs were determined by SEC and SS signal from 14C-IPP. However, her findings support the notion of a living-like
polymerization.
Figure 2.4.4 - Experimental MW results from Cornish et al.’s in vitro NR system for three types of WRPs (Fig tree, Guayule, and Hevea) a) 0.25 µM FPP, b) 2.5 µM FPP.122
Her group studied molecular weight regulation using 14C-labeled monomer and
3H-labeled initiator in vitro with WRPs from Hevea, guayule and Ficus elastica.122 Using dual-labeled liquid scintillation spectrometry they showed that the latter produced twice as high MW NR in vitro than in vivo. Hevea and guayule WRPs, on the other hand,
produced much lower MW NR in vitro than in vivo. Thus MW regulation in NR biosynthesis remains unknown.
39
In summary, NR can be produced in vitro. However, the very complicated
process to isolate the active rubber transferase and synthesize the monomer renders this
process commercially not viable. Therefore it would be highly desirable to devise a
biomimetic process to produce an NR equivalent. Today, NR remains irreplaceable in
many important applications.
2.5 In Vitro Biosynthesis Using Modified Synthetic Initiators
Early studies of prenyltransferases often involved 32P-labeled isoprenoid initiators, given the ease of synthesis of these compounds.123, 124 However, since 32P was readily lost due to the prenylation mechanism and labile nature of the pyrophosphate group, the use of such compounds provided mixed results. Subsequently researchers tried to use traceable modified synthetic initiators. Indeed, prenyltransferases were found to be able to recognize some modified synthetic initiators. In 1985 Baba et al. utilized (E,E)-
2diazo-3-trifluoropropionyloxy geranyl pyrophosphate (DATFP-GPP, Figure 2.5.1) to isolate and identify a 30,000 Da protein subunit to be the binding site for the isoprenoid initiators in undecaprenyl pyrophosphate synthase.125 The authors determined the binding
efficiency by adding synthetic GPP and 14C-labeled IPP to in vitro NR biosynthesis.125
They have found that the binding efficiency for DATFP-GPP + 14C-labeled IPP was
~54% of that of the GPP + 14C IPP control experiment.125 The synthetic initiator with the
shorter C5 DMAPP allylic pyrophosphate (DATFP-DMAPP) was not able to bind to the
active site as no 14C IPP was found to be incorporated.125
40
O 3H
F3C OPP O
N2
Figure 2.5.1 – Chemical structure of DATFP-GPP
While the DATFP-analogues accurately mimicked FPP, they suffered from low affinity and required prolonged short wavelength UV irradiation for photoactivation.
Distefano and Cornish et al. later developed a number of analogues of farnesyl and geranylgeranyl diphosphates containing a benzophenone chromophore for photoaffinity purposes.106 McMahan et al. then studied the benzophenone-modified diphosphate
analogues in three rubber-producing WRPs (Guayule, Hevea, and Fig tree).126 The ketone
group in benzophenone undergoes C-H bond insertion reaction upon excitation with 350
nm wavelength light. This covalently attaches the tracer to a variety of functional groups
present in the enzyme. The benzophenone-modified-FPP was observed to bind to the
active site of prenyltransferases. DMAPP analogues were less reactive, and GPP-
analogues were the least reactive.106
In this thesis we will present the synthesis of a modified initiator di-isobutylene-
neryl pyrophosphate (Figure 2.5.2). This is the model of a polyisobutylene-farnesyl
pyrophosphate macroinitiator that the Puskas group plans to investigate in NR
biosynthesis.
41
O O O O OPP Nerol-PP-DVA-TMP
Figure 2.5.2 – Chemical structure of di-isobutylene-neryl pyrophosphate.
2.6. Biomimetic Polymerization of IP
Biomimicry (from bios, meaning life, and mimesis, meaning to imitate) is a new
discipline that studies nature's best ideas and then imitates these designs and processes to
solve human problems.127 The core idea is that nature, imaginative by necessity, has
already solved many of the problems we are grappling with. Animals, plants, and
microbes are the consummate engineers. They have found what works, what is
appropriate, and most important, what lasts here on Earth. After 3.8 billion years of
research and development, failures are fossils, and what surrounds us is the secret to survival.
Based on the new understanding of NR biosynthesis Puskas et al. investigated the
cationic polymerization of isoprene (IP) initiated by allylic cations generated through
128 ionization of dimethylallyl bromide (DMABr) by TiCl4. (Figure 2.6.1) Using this
strategy, 1,4-oligoisoprene carrying a dimethyl allyl head group was produced in both cis- and trans- configurations, together with cyclized sequences.
42
Figure 2.6.1 – Biomimetic initiation of IP polymerization from Puskas et al.128
In a 2009 follow up study by Puskas and Deffieux et al., DMABr was replaced with dimethyl allyl alcohol (DMAOH) as the initiator.129 The authors attempted the polymerization in bulk, methylcyclohexane, hexanes, and dichloromethane at -40 to 20
oC. The resulting polymers were in oligomers with MWs of 500~1300 g/mol.129 The unsaturation retained in the oligomers was approximately 55%.129 The authors found that high IP conversions were found in less polar media and chain transfers occurred as Mns decreased without the presence of DtBP (2,6-di-tert-butyl pyridine) proton trap. NMR spectra showed that the unsaturation were mostly in trans-1,4 configuration.129
The polymerization of DMAOH was later studied with B(C6F5)3 as the co-
129 initiator in 2011. B(C6F5)3 used in this study is a Lewis acid (LA) with relatively inert
B-C bonds. Many boric LA decompose with the formation of B-F bonds. The authors initiated DMAOH with B(C6F5)3 and studied the resulting compounds. The authors found that the presence of DtBP affected the polymerization. In one case, the LA successfully cationized DMAOH for polymerization; however, it is also possible that DtBP led to elimination to generate IP monomer in situ to result in oligomerization.129
Puskas and Deffieux et al. then investigated the carbocationic polymerization of
IPOH (3-methyl-3-buten-1-ol) initiated by dimethyl allyl alcohol with BF3·2H2O as the co-initiator.130 (Figure 2.6.2). This chemical scheme was a synthetic analogue of NLCP described in Chapter 2.3.6. The pyrophosphate end group of NLCP was replaced by an 43 alcohol group. The polymerization proceeded to polymerize IPOH to yield oligomers
~1000 g/mol with Mw/Mn ~1.3. The structure of the product was quite complex and
MALDI-ToF mass spectrometry (MS) revealed that the reaction initially proceeded by
1,2-addition of monomer followed by chain transfer .130
Figure 2.6.2 – Possible carbocationic polymerization pathways for IPOH.129
In 2011, the cationic polymerization of IP using the 1-(4-methoxyphenyl)ethanol
/B(C6F5)3 initiating system in solution (dichloromethane or α,α,α-trifluorotoluene) and in
aqueous media (suspension, dispersion, or emulsion) was investigated by Puskas and
Deffieux et al.131 The authors observed that the reaction proceeded by controlled initiation, followed by irreversible termination in organic solvents.131 This resulted in polymers with Mn ~ 5000 g/mol, Mw/Mn ~2.5, and high content of intact double bonds
44
(~70%) in the polymer backbone. When using α,α,α-trifluorotoluene as the solvent, the
synthesis of polyisoprene resulted in chains with Mw/Mn ~1.4 and higher content of intact
double bonds (72~88%).131 When the polymerization was initiated with a trace amount of
water, polyisoprenes with fairly high molar mass (Mn ~18,000 g/mol) and Mw/Mn <2.4
were obtained. In aqueous media, the cationic polymerization of isoprene with 1-(4- methoxyphenyl)ethanol/B(C6F5)3 proceeded without any side reactions (cyclization, branching); however, only up to 60% monomer conversion was observed. PIPs with low
131 Mn (~1,200 g/mol) and Mw/Mn ~1.7 were obtained. NMR spectroscopy and MALDI-
Tof revealed that the unsaturation were almost exclusively in trans-1,4 configuration (92-
96.5%).
Figure 2.6.3 – Chemical scheme of cationic polymerization of IP with 131 1-(4-methoxyphenyl) ethanol as the initiator and B(C6F5)3 as the co-initiator.
This thesis conducts cross-disciplinary studies of NR biosynthesis. The
biochemistry of plants is distinctive from other genus of life because plant biochemical pathways tend to be particularly flexible and responsive to changes in the plant’s environment, both as a survival mechanism and as a mean of making optimum use of limiting resources.132 In the year 2000, enzymes are known to catalyze about 4,000 bio- transformations.133 We will investigate NR biosynthesis and bioemulative NR systems.
45
CHAPTER III
EXPERIMENTAL
3.1 Materials
Nerol (>98.0%, TCI America), geraniol (>96.0%, TCI America), 3,4- dihydropyran (DHP, 99%, ACROS Organics), pyridinium p-toluenesulfonate (PPTs,
>98.0%, TCI America), tert-butyl hydroperoxide (TBHP, t-BuO-OH, 70% in H2O, TCI
America), selenium dioxide (SeO2, 99.8%, Sigma Aldrich), sodium hydride (NaH, 95%,
Sigma Aldrich), were used as received. Triphenylphosphine (PPh3), tetrabromomethane
(CBr4), disodium dihydrogen pyrophosphate (Na2H2P2O7), ammonium hydroxide
(NH4OH), 40% (w/w) aqueous tetra-n-butylammonium hydroxide (NBu4OH), 1-bromo-
3-methyl-1-butene, tris(tetra-n-butylammonium) hydrogen pyrophosphate
((NBu4)3HP2O7, >97%), potassium tert-butoxide (95%), allyltrimethylsilane (ATMS,
98%), and 9-borabicyclo[3.3.1]nonane (9-BBN, 0.5 M in THF), hydrogen peroxide (30% w/w in H2O) were purchased from Aldrich and used as received. Salicylic acid, N-
bromosuccinimide (NBS, >99%), dimethyl sulfide ((CH3)2S, >99%) and p- toluenesulfonyl chloride (TsCl, >98.5%), divinyl adipate (DVA, > 98%) were purchased from TCI America and used as received. Celite was purchased from Fisher. Candida antarctica lipase B (CALB, immobilized on a macroporous acrylic resin, Novozym® 435,
Sigma) and Dowex AG 50W-X8 cation-exchange resin (100-200 mesh, hydrogen form) was purchased from Sigma. Tetrahydrofuran (THF, 98.5%), dichloromethane (CH2Cl2, 46
99%) and toluene (99.2%) were distilled over calcium hydride (Aldrich) before use wherever noted. Hexanes (98.5%) and ethyl acetate (≥ 99.5%) were purchased from
EMD and was distilled over sodium and benzophenone before use. Thin layer
chromatography (TLC) silica plates (Dynamic Absorbent Co.) and alumina plates
(Sigma-Aldrich) were used as received. 2,2-dimethyloxirane (IBEpx, >97.0%), 2-
methyloxirane (PPEpx, >99.0%) and di-t-butylpyridine (DtBP, >98.0%) were purchased
from TCI America and used as received. 2-methylpropene (isobutylene (IB), >99%) and
chloromethane (MeCl, >99.5%) were obtained from ExxonMobil. IB and MeCl were dried by passing the gas through a column filled with BaO and CaCl2. Titanium (IV)
tetrachloride (TiCl4, 99.9%) was purchased from ACROS Organics and from Sigma-
Aldrich and used as received. Methanol (99.8%) was purchased from Mallinckrodt
Chemicals and used as received. Sodium bicarbonate (99.7%) and anhydrous magnesium
sulfate (98.0%) were purchased from EMD Chemicals USA and used as received.
Tris-HCl (Tris(hydroxymethyl) aminomethane hydrochloride buffer was obtained
from Sigma-Aldrich and TCI America and used as received. Isoprene (IP, 99%),
stabilized with 100 ppm p-tert-butylcatechol, was obtained from Sigma-Aldrich and used
as received. HPLC grade tetrahydrofuran (THF) was obtained from Fisher Scientific and
was freshly distilled over sodium and benzophenone before use. HPLC grade THF was
also used for the SEC system.
47
3.1.1 Preparation of Washed Rubber Particles (WRP)
The latex of Hevea brasiliensis (RIMM 600 and IAC40) was collected from
research plantation trees at the Regional Centre of Votuporanga (São Paulo State, Brazil),
immediately stabilized, then shipped on dry ice to where the USDA (United States
Department of Agriculture) and stored at -80°C until use. WRP was prepared at the
USDA. The frozen latex was thawed to room temperature and placed on ice. Wash buffer
(100mM tris-HCl, 5 mM dithiothreitol (DTT) and 0.1 mM 4-(2-Aminoethyl)
benzenesulfonyl fluoride hydrochloride (AEBSF, pH = 7.5) was added to the latex and
the diluted latex was divided into 250 mL aliquots. The latex was then centrifuged at
3000 rpm for 10 min at 4oC. The top fraction was collected and transferred into fresh
wash buffer, and centrifuged at 5000 rpm for 10 min at 4oC. The same procedure was repeated with centrifugation at 7000 rpm for 10 min at 4oC. The top fraction was labeled
1X WRP. This washing/centrifugation procedure was repeated for the 1X WRP and the
sample was labeled as 2X WRP. Similar procedure was followed with 2X WRP to obtain
3X WRP. 3X WRPs were used for all in vitro experiments in this thesis. The WRPs were mixed with a small amount of wash buffer and 10% glycerol, and the latex was added into liquid nitrogen drop-wise using a pipette. The small beads forming in the liquid nitrogen were stored at -80°C to preserve the enzymatic activity. The latex and WRP samples were shipped to University of Akron on dry ice and stored at -80°C until use.
48
3.2 Procedures
Procedures for in vitro NR biosynthesis, model reactions, and preparation of the synthetic macroinitiator are discussed in the following sections.
3.2.1 in vitro Natural Rubber Biosynthesis (Hevea WRP) 3.2.1.1 Small Scale Synthesis (USDA)
In vitro experiments were carried out in wells of 96-well filter plates (Millipore
Durapore membrane 0.65 μm) using WRP-1. The reaction volume was 20 μL comprising of 2 μL of buffer (100 mM Tris-HCI, pH 7.5, 1.25 mM MgSO4, 5 mM DTT), 0.4 μL
(4×10-8 mol) of 100 mM IPP, 0.6 μL (6×10-8 mol) of 1mM FPP and 2 mg of WRP-1from
RRIM 600 in 17 μL of water. 5 hrs and 24 hrs reaction times were used at 25oC in an incubator. The reactions were stopped by adding 40 μL (3.2×10-6 mol) of 80 mM EDTA.
The filter plate was vacuumed and then washed two times with 150 μL water then once with 95% ethanol, then oven-dried at 37oC for 30 minutes.
3.2.1.2 Large Scale Synthesis (USDA)
One larger scale reaction was performed in 3.8 mL buffer (100 mM Tris-HCl, 1.25
-7 mM MgSO4, 5 mM DTT, 0.1 mM AEBSF, pH 7.5) containing 0.1 mM (3.8×10 mol) IPP,
15 μM (5.7×10-8 mol) FPP and 76 mg WRP-3 from RRIM 600. The reaction was run at room temperature with gentle stirring and was stopped by adding 40 mM EDTA (330 μl of 0.5 M
EDTA) after 24 hrs incubation. A blank was also prepared that had no FPP and IPP.
49
3.2.1.3. “Bioemulative” Experiments Using Synthetic Isoprene with WRP-3
(USDA)
Together with the reaction in 3.2.1.1 one reaction was performed in 3.8 mL buffer
(100 mM Tris-HCl, 1.25 mM MgSO4, 5 mM DTT, 0.1 mM AEBSF, pH 7.5) and 15 μM
(5.7×10-8 mol) FPP and 76 mg WRP-3 from RRIM 600, to which 26mg (0.38 mmol) IP was added. The reaction was run at room temperature with gentle stirring and was stopped by adding 40 mM EDTA (330 μl of 0.5 M EDTA) after 24 hrs incubation.
3.2.2 Experiments with IAC40 latex and WRP 3.2.2.1 Solids Content Determination for Latex and WRP
Solids content of IAC40 latex and WRP were determined by three different methods: 1) simply freeze drying the latex and WRP in vials without washing; 2) washing three times with buffer (100mM tris-HCl, pH = 7.5) and MQ water after self- coagulation, then freeze-dried to constant weight; and 3) by precipitating the NR latex and WRP into chilled methanol (4 oC). The precipitated polymer was white. The polymer was then washed with buffer (100mM tris-HCl, pH = 7.5) and MQ water to remove water-soluble solids and freeze-dried in the vacuum oven to constant weight.
3.2.2.2 In situ Raman monitoring (UAkron)
0.5 g active IAC40 WRP or IAC40 latex was sealed in glass vials (Fischer
Scientific, 1ml silanized glass vials) using a crimper. After the injection of isoprene (IP)
(0.102 g, 0.15 mL, 1.50 mmol) through the hermetic cap, the contents were vigorously shaken for one minute to ensure good mixing. The reactions were monitored by in situ
Raman spectroscopy. After incubation for 24 hours, the product was washed three times
50
with buffer (100mM tris-HCl, pH = 7.5) and de-ionized (DI) water. The rubber was then
freeze-dried until constant weight. The initial rubber weight was obtained by washing the
rubber, which was self-coagulated from latex/WRP at room temperature, three times with buffer (100mM tris-HCl, pH = 7.5) and de-ionized water, then freeze-drying till constant
weight. The initial rubber content data for the WRP and latex are based on the average of
three independent measurements (latex = 19.1% ± 0.4%, WRP = 17.8% ± 0.3%).
3.2.2.3 Micro-Raman Spectroscopy
The laser source was Lexel Raman Ion Krypton laser and the excitation wavelength was set at 647 nm. Raman signal was collected by a Horiba Jobin-Yvon
Labram HR single monochromator equipped with a nitrogen-cooled CCD camera. The sealed polymerization vial was fixed under a long-working distance 50X objective from
Mitutoyo with Numerical Aperture (NA) = 0.42. Spectra were collected for five minutes
for every data point, and then the laser was blocked for five minutes to avoid heating and fluorescence. This sequence was repeated for the duration of the first six hours of the experiment. The samples were incubated for a total of 24 hours. The position of the monochromator in most of the measurements was fixed at 1500 cm-1 to ensure the
capture of the major Raman modes characteristic of the C=C bonds in IP and PIP. The
schematic setup of the instrumentation is shown in Figure 3.2.1 and the actual
instrumentation is shown in Figure 3.2.2.
51
Figure 3.2.1 - Experimental set-up for the in situ Raman measurements.
a) b) Figure 3.2.2 -.Micro-Raman instrumentation in the Sokolov lab: a) before the experiment b) during in situ monitoring.
3.2.2.4 Experiments under CO2 atmosphere (UAkron)
1 mL silanized glass vials (Fischer Scientific), containing the latex or WRP??
Which ?, were sealed. For the experiments under CO2 atmosphere, the vials were purged with CO2 from dry ice and the pressure was regulated using an exit bubbler, as depicted in Figure 3.2.3. For samples denoted as KC_121109_W_IP1 (CO2/50X) and 52
KC_121409_W_IP3(CO2/50X) in Table 4.2.4, ~0.5 g of active IAC40 WRP or IAC40 latex and 0.10 g IP (0.15 mL, 1.50 mmol) were injected through the hermetic cap. For samples denoted as KC_120809_L_IP1 (CO2/50X) and KC_121109_W_IP2 (CO2/50X)
(Table 1), ~0.65 g of IAC40 WRP or IAC40 latex and 0.13 g of IP (0.19 mL, 1.95 mmol) were injected into the vials through the hermetic cap. The contents were then vigorously shaken for one minute to ensure good mixing. The rationale for increasing the reaction volume for the last two experiments (i.e. KC_120809_L_IP1 (CO2/50X) and
KC_121109_W_IP2 (CO2/50X)) was due to the horizontal configuration of the sample vials during Raman measurement. There were several incidences where the NR sample detached from the vial surface and the laser had to be re-aligned and re-focused when
placed in a horizontal position. By increasing the reaction volume, we hoped to prevent
detachment from the glass vial surface. It is important to note that the only variant was
the reaction volume. Therefore, the mole ratio between the latex/WRP and the IP
remained constant. After incubation for 24 hours, the products were washed three times
with buffer (100mM tris-HCl, pH = 7.5) and Milli-Q (de-
Figure 3.2.3 - Methodology to exchange the atmosphere within the closed vial.
53
3.2.2.5 “Bioemulative” experiments using deuterated isoprene (UAkron)
The deuterated isoprene(DIP) monomer (Oakridge National Lab, TN,
synthesized: 6/3/2008) was sealed in a vacuumed ampule and used as received. The
purity of the sample was determined by Gas Chromatography (GC) prior to use and the
sample was found to be 85.1% pure. 0.5 g active IAC40 latex were sealed in glass vials
(Fischer Scientific, 1ml silanized glass vials) using a crimper. 0.102g mixturesof isoprene
(IP) and D-IP (0.15 mL, 1.50 mmol) were injected into the vials through the hermetic cap with the following concentrations at 100% D-IP, 50/50 D-IP/IP and 100% IP. Two incubations were performed for each mixture. The contents were vigorously shaken for one minute to ensure good mixing. The 100% D-IP experiment was monitored by in situ
Raman spectroscopy. After incubation for 24 hours, the product was washed three times with buffer (100mM tris-HCl, pH = 7.5) and de-ionized water. The rubber was then freeze-dried until constant weight. The initial rubber weight was 19.1% ± 0.4% for latex and 17.8% ± 0.3% for WRP, which were determined previously as described in 3.2.2.1.
3.3 Synthesis of Macroinitiator
3.3.1 Synthesis of Protected Nerol (PN, product 2 in Figure 4.4.1 in Section 4.4)
A solution of nerol (10 g, 65 mmol) in dichloromethane (65 mL) was placed in a
250 mL one-neck round-bottom flask equipped with a condenser and a magnetic stirrer. di-hydropyran (6.55 g, 78 mmol) and pyridinium p-toluenesulfonate (1.63 g, 6.5 mmol) were added to the reactor and the resulting solution was stirred and thermostated at 27°C for 4 hours. Then the reaction mixture was concentrated using a rotary evaporator under reduced pressure, diluted with ethyl acetate and washed with saturated aqueous sodium 54
bicarbonate solution. The organic layer was dried over magnesium sulfate, filtered and
concentrated to yield transparent oil. The residue was purified by flash chromatography
(63-200 µm) eluent: ethyl acetate/hexane, 1:8 v/v; (silica TLC: Rf = 0.7) on silica gel to
yield PN (~14 g, 90%). The product was analyzed by 1H and 13C NMR spectroscopies.
3.3.2 Synthesis of Protected Nerol-OH (PN-OH, product 3)
A solution of PN (13 g, 55 mmol) in dichloromethane (70 mL) was placed in a
250 mL one-neck round-bottom flask equipped with a condenser and a magnetic stirrer.
tert-butyl hydroperoxide (24 mL, 173 mmol), selenium dioxide (0.61 g, 5.5 mmol) and
salicylic acid (0.76 g, 5.5 mmol) were added to the reactor and the resulting solution was
stirred at 30°C for 24 hours. Diethyl ether and water were added and the layers were
separated. The organic phase was washed with water three times. The combined organic
phase extracts were washed twice with saturated sodium bicarbonate aqueous solution,
dried over anhydrous magnesium sulfate, filtered, and concentrated by rotor evaporation.
The crude oil was purified by flash chromatography (63-200 µm, eluent: ethyl
acetate/hexane, 1:5 v/v; silica TLC: Rf = 0.15) on silica gel to yield PN-OH (~3 g, 25%)
(The literature reports ~30% yield for compounds with similar chemical structures103).
The product was analysed by 1H and 13C NMR spectroscopies.
3.3.3. Synthesis of Protected Nerol Tosylate (PN-Ts, product 4)
TsCl was recrystallized in ethyl acetate before use. In a 250mL round bottom flask, PN-OH (9.98g, 39mmol, a combination of pure PNOH from several syntheses),
BnNMe2 (0.522g, 3.86mmol), and K2CO3 (8.142g, 59mmol) were added in 30mL of
distilled water at room temperature. A stock solution of 1M KOH was made to maintain
55
pH of 10 during the reaction. The mixture was stirred vigorously and TsCl (11.250g,
59mmol) was added in 10 portions, every 6 minutes over the first hour. Immediately after
the addition of TsCl, drops of KOH were added to maintain the pH at 10. The pH was
monitored using a Mettler-Toledo portable digital pH meter. After the addition of TsCl,
the reaction was monitored with TLC (silica) and continued until there was no more PN-
OH (Rf = 0.1) spot. The Rf value of PN-Ts is 0.5 with 15:1 Hx/Ether as eluent. 1.00g of
N,N-dimethylethylene diamine was added to the mixture and stirred for 10 minutes to
react with the excess TsCl and quench the reaction. Water was added and the organic
phase was extracted with ethyl acetate. The organic fraction was washed with water and
brine two times and dried over anhydrous MgSO4. The crude product was purified by flash chromatography on silica gel to yield PN-OTs (12.62 g, 92%): silica TLC
(hexane/ether, 15:1, v/v) Rf = 0.5.
3.3.4 Synthesis of Polyisobutylene-Protected Nerol (PIB-PN, product 5)
In the glove box, sodium hydride (0.024 g, 1.0 mmol) and PIB-OH (5,800 g/mol,
Mw/Mn = 1.06, 1.02 g, 0.18 mmol) was added to 25 mL of distilled THF in a 100 mL
three-neck round-bottom flask. The mixture was stirred by a mechanical stirrer and PN-
Ts (1.2 mmol) was added drop-wise and the mixture was stirred for 5 days. Then the reaction mixture was slowly poured into water at 3°C, washed with a sodium sulfite solution (Na2SO3), and extracted 3 times with diethyl ether. The organic layers were washed twice with water, once with a saturated solution of sodium chloride, dried over anhydrous magnesium sulfate, filtered, and concentrated with a rotary evaporator. The polymer was analyzed by 1H and 13C NMR spectroscopies. The product was purified by
56
column chromatography (Hexane/Ethyl acetate, 10:1, v/v) three times due to tailing on
silica gel to yield PIB-PN (0.59 g, 60%).
3.3.5 Synthesis of Polyisobutylene-Nerol (PIB-Nerol, product 6)
A solution of PIB-PN (0.55 g, 0.09 mmol) in isopropyl alcohol (15 mL) and
hexane (7.5 mL) was placed in a 50 mL one-neck round-bottom flask equipped with a condenser and a magnetic stirrer and pyridinium p-toluenesulfonate (0.3 g, 1 mmol) was
added to the flask and stirred at room temperature for 20 hours. The polymer was precipitated in chilled methanol and washed with DI water three times. The polymer was freeze-dried. The residue was purified by column chromatography (eluent: Hx/EA, 10:1 v/v) on silica gel to yield PIB-Nerol (~0.53g, 98%). The product was analyzed by 1H and
13C NMR spectroscopies.
3.3.6 Synthesis of Polyisobutylene-Nerol-Bromide (PIB-Nerol-Br, product 7)
A solution of PIB-Nerol (0.50 g, 0.0DATF8 mmol) in dichloromethane (5 mL)
was prepared. In a 50 mL two-neck round-bottom flask equipped with a condenser and a
magnetic stirrer, dichloromethane (25 mL), NBS (0.888 g, 5.0 mmol) and Me2S (0.62g,
10 mmol) were added and chilled in a isopropyl alcohol/dry ice bath at -40 oC. A white
precipitate was formed at the bottom of the flask. The stirring speed was increased to
create a white suspension, and the solution of PIB-Nerol was injected through the rubber
septum. The reaction mixture was left stirring for one hour at –40 oC. The polymer was
precipitated in chilled methanol and washed with DI water and saturated sodium
bicarbonate solution three times. The polymer was then freeze-dried. The residue was
57
purified by column chromatography (eluent: Hexane/Ethyl aceate, 10:1 v/v) on silica gel
to yield PIB-Nerol-Br (~0.27g, 60%). The product was analyzed by 1H and 13C NMR spectroscopies.
3.3.7. Synthesis of Tris(tetra-n-butylammonium) Hydrogen Pyrophosphate
[(NBu4)3HP2O7]
The procedure was reported by Poulter et al.134 A solution of 3.33 g (15 mmol) of
disodium dihydrogen pyrophosphate Na2H2P2O7 in 41 mL of 0.104N aqueous solution of
ammonium hydroxide NH4OH (4.26 mmol) was passed through a column (Length:
20cm; Ø: 1cm) of Dowex AG 50W-X8 cation-exchange resin (100-200 mesh, hydrogen
form). The free acid was eluted with 90 mL of deionized water, and the resulting solution
(pH = 1.5) was immediately titrated to pH 7.3 with 40% (w/w) aqueous tetra-n-
butylammonium hydroxide NBu4OH. The resulting solution was concentrated under vacuum and then dried by lyophilisation to yield 13g of a hygroscopic white solid (96%).
The product was analyzed by 1H, 13C and 31P NMR spectroscopies.
58
3.3.8. Synthesis of Nerol-Pyrophosphate (Nerol-PP, model of product 8) This model reaction proceeded in the University of Bordeaux, France following
procedures adapted from Chen et al135. 0.50 g (3.3 mmol) of Nerol-Br and 3.48 g (4
mmol) of (Bu4N)3HP2O7 were solubilized in anhydrous acetonitrile under nitrogen atmophsere. The reaction was sitrred for 6 hours and then was concentrated under reduced pressure and a few drops of MQ water were added. The solution was then passed through Dowex AG50X8 ion exchange column (IXC) (NH4+ form). After the column the
solution was directly injected into LC (mobile phase: aceonitrile). Thedesired fration was
collected at the and and the product was freeze-dried into a white powder (0.94 g, 0.9
mmol, 27% conversion).
3.3.9. Synthesis of Protect Nerol-Divinyl Adipate (PN-DVA, Product 9)
Divinyl adipate (2.3 g, 12 mmol, [vinyl] 4 eq.) was added to an air-free, nitrogen-
purged, round-bottom flask containing PN-OH (Product 3, 1.01 g, 4.4 mmol), CALB (13
mg, 10% wt) and THF (1.5 mL). The mixture was stirred for 24 hours at 50 °C and
monitored by TLC (silica). After filtering off the enzyme with a 0.45 µm PTFE syringe
filter, the oil was concentrated with a rotary evaporator and purified by silica flash
chromatography twice. (elutent: Hexane/THF, 4:1, v/v, Rf = 0.5) The resulting oil had a
slightly yellow hue and the structure was analyzed by 1H and 13C NMR spectroscopies.
(Yield: 1.3g, 80%)
3.3.10 Synthesis of Trimethyl Pentyl Chloride (TMPCl, Product 10)
Sodium chloride (NaCl, 45 g, 0.77 mol) was placed into a 500 mL, three-necked, round-bottom flask. Concentrated sulfuric acid (65 mL, 0.65 mol) was added to the NaCl 59
very slowly from a dropping funnel to form HCl gas. The HCl gas was bubbled into neat
2,4,4-trimethyl-1-pentene (TMP-1, 11.6 g, 105 mol) in a round-bottom flask which was
kept in an ice-water bath. The reaction flask was connected to a trap and to another flask
containing concentrated sodium hydroxide solution to neutralize the unreacted HCl acid.
After 24 hours, TLC was checked and more NaCl and concentrated sulfuric acid was added to the setup until reaching 100% conversion observed by TLC over ~36 hours.
After work up, the reaction yielded 13.2 g of TMPCl (89 mmol, ~85%, loss of product from filtering)
3.3.11. Synthesis of Allyl Trimethyl Pentane (TMP-allyl, Product 11)
A 250-mL, three-necked, round-bottom flask equipped with an overhead mechanical stirrer was immersed in a hexane bath kept at -80 °C. TMPCl (4.01 g,
46mmol), DtBP (0.15 g, 2 mmol) were added to the reaction flask which was charged with a 60/40 (v/v) mixture of hexane (54 mL) and MeCl (36 mL). The reaction commenced with the rapid introduction of a pre-chilled stock solution of TiCl4 (10.1 g,
365 mmol). Amount of TiCl4 or ATMS used in this reaction was calculated depending on
the amount of TMPCl used (molar ratio [TiCl4]/[TMPCl] = 8). After stirring the reaction
mixture for 20 minutes, the intermediate was reacted with pre-chilled ATMS (6.21 g,
460mmol, molar ratio [ATMS]/[TMPCl] = 10). The solution was stirred for another 40
minutes in the glove box. The flask was taken out of the box and saturated aqueous
NaHCO3 solution was slowly added to the solution while the MeCl evaporated. The
solution was washed three times with distilled water and dried over anhydrous MgSO4.
60
The solvent was removed using a rotary evaporator and the oil was freeze-dried. (Yield:
4.12 g, conversion: 90%).
3.3.12. Synthesis of Trimethyl Pentane-OH (TMP-OH, Product 12)
Hydroboration followed by alkaline oxidation is the general method used to
convert PIBs with allyl (PIB-CH2-CH=CH2) end groups to the corresponding PIBs with
primary alcohol functionalized end groups. The same procedure was applied for TMP-
allyl. TMP-allyl (4.00 g, 24 mmol) was dissolved in distilled THF (100 mL) and added
drop-wise to an ice chilled THF solution of 9-BBN (17.8 mL, 8.9 mmol, 0.5 mol/L)
under an inert atmosphere (N2) over 30 minutes. After stirring the reaction mixture at
room temperature for five hours, 25% w/w KOH solution in methanol (1.5 g in 6 mL of
methanol) followed by 30% v/v H2O2 solution(2.7 mL) were added drop-wise to the
reaction mixture while maintaining the reaction temperature at 3 ºC. The reaction
mixture was then allowed to react for 2 hours. Hexane (100 mL) was added to the
solution, stirred for five minutes and poured into 200 mL saturated potassium carbonate
solution. The organic layer was washed several times with distilled water and dried with anhydrous MgSO4. The solution was filtered and rotary evaporated to dry. (Yield: 3.12 g,
conversion: 72%).
3.3.13. Synthesis of Protected Nerol-Divinyl Adipate-Trimethyl Pentane (PN-DVA-TMP, Product 13)
TMP-OH (0.78 g, 4.6 mmol) was added to an air-free, nitrogen-purged, round-
bottom flask containing PN-DVA (2.03 g, 5.0 mmol), CALB (17 mg, 10% wt) and THF
(10.0 mL). The mixture was stirred for 24 hours at 50 °C and monitored by TLC. After
61
filtering off the enzyme with a 0.45 µm PTFE syringe filter, the oil was concentrated with
a rotary evaporator and purified by silica flash chromatography twice. (elutent:
Hexane/THF, 4:1, v/v, Rf = 0.5) The chemical structure of the transparent resulting oil was analyzed by 1H and 13C NMR spectroscopies. (Yield: 1.84 g, 3.45 mmol, 70%)
3.3.14. Synthesis of Nerol-Divinyl Adipate-Trimethyl Pentane (Nerol-DVA-TMP,
Product 14)
A solution of PN-DVA-TMP (1.05 g, 2.0 mmol) in isopropyl alcohol (10 mL) and
hexane (5 mL) was added to a 25 mL one-neck round-bottom flask equipped with a
condenser and a magnetic stirrer. Pyridinium p-toluenesulfonate (PPTs, 0.2 g, 0.8 mmol)
was added to the reaction mixture and the reaction was stirred at room temperature for 20
hours. The reaction mixture was concentrated with a rotary evaporator which led to the
formation of white crystals of pyridinium p-toluenesulfonate at the bottom of the flask.
Petroleum ether was added to dissolve the product but not the PPTs. The product was
then washed with DI water three times. The product was purified by silica flash
chromatography (eluent: Hexane/THF, 4:1, v/v) on silica gel to yield N-DVA-TMP
(Yield = 0.8 g, 90%). The product was analyzed by 1H and 13C NMR spectroscopies.
3.3.15. Synthesis of Nerol-Bromide-Divinyl Adipate-Trimethyl Pentane (Nerol-Br-DVA
-TMP, Product 15)
The bromination of Nerol-DVA-TMP to Nerol-Br-DVA-TMP proceeded in
dichloromethane at -40 oC using N-bromosuccinimide (NBS) and dimethyl sulfide.
Nerol-DVA-TMP (0.55 g, 1.2 mmol) and NBS (0.27 g, 1.5 mmol) were added to CH2Cl2 and left stirring for 20 minutes before warming the reaction flask to 0 oC. After the
62
o temperature stabilized at 0 C, dimethyl sulfide (Me2S, 0.1 g, 1.6 mmol) was injected and
the reaction proceeded for 6 hours. The reaction yielded ~0.4 g (0.8 mmol) of Nerol-Br-
DVA-TMP, which corresponded to ~65% conversion. The product was purified by
column chromatography (eluent: Hexane/Ethyl acetate (EA), 10:1, v/v) (Rf = 0.25 for
Nerol-Br-DVA-TMP, Rf = 0.1 for Nerol-DVA-TMP).
3.3.16. Synthesis of Nerol-Pyrophosphate-Divinyl Adipate-Trimethyl Pentane (Nerol-PP-
DVA-TMP, Product 16)
The phosphorylation of Nerol-Br-DVA-TMP to Nerol-OPP-DVA-TMP proceeded in air-free conditions for 6 hours, which was in accordance with the literature.
Nerol-Br-DVA-TMP (0.3 g, 0.6 mmol) and (Bu4N)3HP2O7 (0.9 g, 1 mmol) was added to
2 mL of anhydrous acetonitrile equipped with a magnetic stirring bar. After 6 hours, the anhydrous acetonitrile was evaporated under reduced pressure and a few drops of MQ water were added. The solution was then passed through Dowex AG50X8 ion exchange column (IXC) (NH4+ form).
3.3.17. Synthesis of Nerol-P(O)(OEt)2 (Model Reaction for Phosphorylation).
A solution of Nerol (250 mg, 1.62 mmol) and pyridine (0.16g, 2.02 mmol) in chloroform (5 mL) was added to a 10 mL one-neck round-bottom flask equipped with a
15 mL additional funnel and a magnetic stirrer. The reaction mixture was chilled to 1 oC
using an ice bath. Diethyl chlorophosphate solution (0.28 g, 1.62 mmol in 1 mL CHCl3) was added to the flask slowly using the additional funnel and the reaction mixture solution was stirred at 1 oC for 4 hours. The reaction was monitored by TLC (silica) (1:3
Hexane/Ethyl acetate). The reaction mixture was concentrated slightly using rotary
63
evaporator and then loaded directly onto a silica gel column (1:3 Hexane/Ethyl acetate) to
separate and purify Nerol-P(O)(OEt)2 (~150 mg, 32%, Rf = 0.34) and Nerol (~125 mg,
50%, Rf = 0.9). Nerol-P(O)(OEt)2was a light yellow oil with some crystals. The product
was analyzed by 31P NMR spectroscopies.
3.3.18. Synthesis of Nerol-P(O)(OEt)2-DVA-TMP (Product 15).
A solution of Nerol-DVA-TMP (0.2 g, 0.44 mmol) and pyridine (0.05g, 0.65
mmol) in chloroform (3 mL) was added to a 5 mL one-neck round-bottom flask equipped
with a 15 mL additional funnel and a magnetic stirrer. The reaction mixture was chilled
to 1 oC using an ice bath. Diethyl chlorophosphate solution (0.1 g, 0.69 mmol in 1 mL
CHCl3) was added to the flask slowly using the additional funnel and the reaction mixture solution was stirred at 1 oC for 4 hours. The reaction was monitored by TLC (silica) (1:3
Hexane/Ethyl acetate). The reaction mixture was concentrated slightly using rotary
evaporator and then loaded directly onto a silica gel column (dichloromethane) to separate and purify Nerol-P(O)(OEt)2-DVA-TMP (~150 mg, 32%, Rf = 0.6) and Nerol
(~115 mg, 50%, Rf = 0.25).
3.3.19. Synthesis of Nerol-PP-DVA-TMP (Product 16).
Under inert atmosphere, a solution of Nerol-P(O)(OEt)2-DVA-TMP (0.15 g, 0.35
mmol) (Bu4N)3HP2O7 (0.8 g, 0.7 mmol) in chloroform (3 mL) was added to a 5 mL one- neck round-bottom flask equipped with a 15 mL additional funnel and a magnetic stirrer.
The reaction was stirred at room temperature for 2 days and was monitored by TLC
(silica) (acetonitrile). The reaction mixture was concentrated slightly vacuum then loaded directly onto a cellulose Whatman CF-11 column (anhydrous acetonitrile) to separate and
64
purify Nerol-P(O)(OEt)2-DVA-TMP (Rf = 0.4) and Nerol-PP-DVA-TMP (~240 mg,
54%, Rf = 0.7).
3.4. Laboratory Techniques and Instrumentation 3.4.1. Air-free Technique
The removal of contaminants (e.g. O2, H2O, CO2) and volatile impurities from the
glassware, solvents, and reagents used was necessary to avoid unwanted reactions for
some steps. This was accomplished by using a Schlenk line and air-free glassware. The
Schlenk line consisted of a 4-port air-free vacuum manifold made of Pyrex® glass tubing.
All connection ports used were Teflon stopcocks. A vacuum pump was connected to one
end of the manifold. A liquid nitrogen trap was placed between the manifold and the
pump to protect the pump oil from solvent contamination. Nitrogen gas (Praxair,
technical grade) was introduced into the vacuum line through the other end of the
manifold. The pressure of the nitrogen gas in the vacuum line was controlled using a
bubbler. A glass drying column packed with anhydrous calcium sulfate and dried
molecular sieves (4Å) was placed between the gas cylinder and the manifold to dry the
nitrogen gas.
3.4.2. Thin Layer Chromatography (TLC)
Silica plates (Dynamic Absorbent Co.) or alumina plates (Sigma-Aldrich) were
used to perform TLCs using different eluents depending on the compounds involved.
Specific conditions are given in the syntheses section. The typical solvents used were
hexanes, ethyl acetate, THF, and diethyl ether. Capillaries were made from disposable
pipettes over propane torch. For a typical TLC experiment, a drop of sample solution was
65
placed on the TLC plate using a capillary and the plate was eluted with the appropriate
solvent(s). The spots were observed using any of the following three methods : (a)
developing the plate by dipping in a solution of phosphomolybdic acid in ethanol
(Aldrich) (b) exposing it to a UV lamp (λ=254 nm) or (c) using an iodine chamber.
3.4.3. Column Chromatography
Column chromatography was used for the purification of compounds. The columns were packed with silica gel as follows: the appropriate eluent (specific conditions are given in synthesis details of each compound) was added to a beaker containing silica gel (Dynamic Adsorbent Inc, 63-200µm, silica gel classic column (Lot#
LB1708)) or alumina (Dynamic Adsorbent Inc, 63-200µm Alumina for DCC). The resulting slurry was quickly poured into a Pyrex® column and the solvent was allowed to drain through the column until its level was just above the surface of silica gel. The column was gently tapped during this time in order to insure that there were no air bubbles in the packed silica gel or alumina. After the column was uniformly packed, the crude product dissolved in a small amount of solvent was carefully loaded onto the column using a pipette. The solution was allowed to drain until the level reached the top of silica gel. A small amount of sand was added carefully to protect the top of the silica column. The eluent was run through the column applying air pressure at the top of the column, resulting in rapid separation of the products and high column performance. In flash chromatography, air pressure was applied. The fractions were analyzed by TLC and the fractions containing the pure product were combined and concentrated using a rotary evaporator under reduced pressure.
66
3.4.4 Size Exclusion Chromatography
Molecular weights (MWs) and molecular weight distributions (MWDs) were
determined by SEC. The SEC system used in this study was a Waters setup equipped
with six Styragel columns (HR0.5, HR1, HR3, HR4, HR5, and HR6) thermostatted at
o 35 C as the stationary phase. Tetrahydrofuran (THF) continuously distilled from CaH2 was used as the mobile phase at a flow rate of 1 mL/min. The list of detectors include a
Wyatt Technology Viscostar viscometer (VIS), a Wyatt Optilab DSP refractive index
(RI) detector thermostatted at 40oC, a Wyatt DAWN EOS 18 angle multi-angle laser light
scattering (MALLS) detector, a Wyatt quasi-elastic light scattering (QELS) and a Waters
2487 Dual Absorbance ultraviolet (UV) detector. (Note: the UV detector was used;
however, the signal intensity was very low to be useful as the injection concentration was
very low. This issue will be addressed in future) Absolute molecular weights and radii of
gyration were determined using ASTRA® V software 5.3.4 and dn/dc = 0.130 reported
for high cis-poly-isoprene.8 The dn/dc value was confirmed with polyisoprene standards
(Mn = 2,450 and 9,870 g/mol and Mw/Mn = 1.02 and 1.03) supplied by Scientific Polymer
Products, Inc. The schematic of the SEC system is shown in Figure 3.4.1. In our experiments, it is important to note that the viscometer was not used because the protein residues left in the rubbers clog the capillaries of the viscometer.
67
Figure 3.4.1. High resolution SEC system at the Puskas Lab.
3.4.5. NMR sample preparation
The dried rubber samples incubated with IP were dialyzed using Nest Group’
SpinDIALYZER (50 μL) with 0.6 μm PTFE membranes (Millipore) in order to separate the insoluble gel fraction and the soluble component. The solution outside the dialysis chamber and the gel within the chamber were concentrated and freeze-dried until constant weight. After freeze-drying, the soluble fraction from the outside chamber (~50-
70 mg) was dissolved in 1 mL of benzene-D6 (Cambridge Isotopes Inc.) or 1 mL of
toluene-D8 (Cambridge Isotopes Inc.) in a 3 mL glass vial. The samples were left to
dissolve in the dark for 6 hours and transferred to NMR tubes.
After incubation with D-IP and freeze drying, ~100 mg of the NR was dissolved
in 4 mL benzene-D6 and then filtered into a pre-weighed vial. The sample was dried with
68
a vacuum pump (Yield: ~50 to 60 mg after drying) and ~1 mL benzene-D6 was added to
make a ~50 mg/mL solution.
3.4.6. 1H NMR procedure
1H NMR was performed using either a 300MHz Varian Mercury NMR or a 500
MHz Varian One NMR instrument 128 scans were taken with d1 (relaxation time) = 10
seconds and 45° pulse angle. The temperature was controlled at 25 °C and the solvents
used were typically benzene-D6, toluene-D8 or chloroform-D. Concentrations of the
sample solutions used for the 1H NMR measurements are listed by the figures. Total
acquisition times are listed in the appendix for each NMR spectrum.
3.4.7. 13C NMR procedure
13C NMR was performed using either a300MHz Varian Mercury NMR or a 500
MHz Varian One NMR instrument. 10,000 scans were taken with d1 (relaxation time) =
10 seconds and 90° pulse angle, as suggested by Tanaka et al.136 The temperature was
° controlled at 25 C and the solvents used were typically benzene-D6, toluene-D8 or
chloroform-D. Concentrations of the sample solution used for the 13C NMR
measurement are listed by the figures.
3.4.8. Gas Chromatography
Gas chromatography (Shimadzu GC-8A) was performed using an Equity-1 fused
silica capillary column, a TCD detector, and a CR501 recorder using He as a carrier gas.
The temperature range was between 80°C to 280 °C and the inject-to-collection delay was
1 minute.
69
3.4.9. Matrix Assisted Laser Desorption/Ionization Time-of-Flight Mass Spectrometry
(MALDI-ToF MS)
MALDI-ToF mass spectra were acquired on a Bruker UltraFlex-III ToF/ToF mass
spectrometer (Bruker Daltonics, Inc., Billerica, MA) equipped with a Nd:YAG laser (355
nm) for verifying the purity and mass distribution of the products. All spectra were measured in positive reflector mode. The instrument was calibrated prior to each measurement with an external poly(methyl methacrylate) (PMMA) standard. Individual solutions of polymer (10 mg/mL) in anhydrous THF (99.5 %, Aldrich), 1,8,9- trihydroxyanthracene matrix (dithranol, 20 mg/mL, 97 %, Alfa Aesar), and silver trifluoroacetate (AgTFA, 10 mg/mL, 98%, Aldrich) in anhydrous THF were mixed in the ratio of polymer:matrix:cationizing salt (1:10:2), and 0.5 µL of the resulting mixture were deposited on microtiter plate wells (MTP 384-well ground steel plate). After evaporation of the solvent, the plate was inserted into the MALDI source. The spectra were obtained in the reflectron mode at an acceleration voltage of 20 kV. The attenuation of the
Nd:YAG laser was adjusted to minimize unwanted polymer fragmentation and to maximize the sensitivity.
3.4.10. Electrospray Ionization Mass Spectrometry (ESI-MS)
ESI mass spectra were acquired with a Bruker Daltonics Esquire-LC ion trap mass spectrometer for the identification of mass. The sample was dissolved in anhydrous
THF (99.5 %, Aldrich) at 1µg/µL, and the resulting solutions were mixed with 1µg/µL solution of sodium trifluoroacetate (98%, Aldrich) as a cationizing agent in THF in the ratio 100:1(sample:salt) (v/v). Experimental conditions: positive mode; dry gas: nitrogen 70
(8 L/min); drying temperature: 300 °C; nebulizer gas: nitrogen (10 psi). The sodium salt solutions were introduced into the ESI source by direct infusion using a syringe pump at a flow rate of 250 µL/h.
71
CHAPTER IV
RESULTS AND DISCUSSION
4.1. In vitro Natural Rubber Biosynthesis
4.1.1. Monitoring the Growth of in vitro Natural Rubber by High-Resolution Size
Exclusion Chromatography (HR-SEC)
Enzymatically active WRP (WRP-1) was isolated from RRIM600 latex as
described in Chapter 3.1.2 RRIM600 stands for Rubber Research Institute of Malaysia –
600, which is a representation of a typical H. brasiliensis clone. The solids content was
measured by drying the WRP-1 at 60 oC for 24 hours, and was found to be 278 mg/mL
(27.8 wt%). The enzymatic activity was determined by procedures in Chapter 3.1.2, in
which the WRP was incubated with 14C-labeled IPP with and without FPP initiator.
Figure 4.1.1 shows the well plates used for in vitro NR biosynthesis. Mau and Cornish112 developed multi-well plate assay to determine the enzymatic activity rapidly. Previously, enzymatic activities of prenyltransferases were determined by incubating the rubber particles with radiolabelled IPP in each individual micro-centrifuge tubes with varying concentration of IPP at a saturated concentration of FPP (or APP initiator).113
72
Figure 4.1.1 – Micro well-plates in which in vitro NR biosyntheses are performed.
In the multi-well method, PVDF filters were placed at the bottom of the wells. In each micro-well, 2 mg WRP samples were incubated with FPP initiator, 14C IPP monomer, and Mg2+ cofactor. (Figure 4.1.2a) After 4 hours, EDTA was added to terminate the reactions. EDTA is a ligand that strongly chelate with metal co-factors
(Mg2+) to quench the reaction. The buffer in the wells was suctioned out of the wells by vacuum and washed repeatedly with water, 1M HCl and 95% ethanol to remove unreacted 14C labeled IPP. (Figure 4.1.2b) The filters were taken out of the wells and placed in scintillation fluid for radioactivity measurements to determine the enzymatic activity.
73
Figure 4.1.2 – An example micro-well and its constituents a) during incubation, b) after incubation.
Using this method, it was found that RRIM600 WRP-1 was able to incorporate
10.3 µmol 14C-labeled IPP per g of dry rubber when incubated with non-labeled FPP synthetic initiator (Figure 4.1.3). In the absence of FPP, 3.0 µmol 14C -labeled IPP per g of dry rubber incorporated. These data agree with activities reported in the literature.118
Figure 4.1.3 – Enzyme activity measurement of RRIM600 WRP-1 using 14C IPP (USDA).
74 Figure 4.1.4 shows the SEC Refractive Index (RI) trace of the toluene-soluble
fraction of WRP-1 from RRIM600. The high molecular weight (MW) region shows a
peak in the 106 g/mol range (1H) with a shoulder at ~105 g/mol. There are four distinct
low MW peaks (i.e. labeled as 1L, 2L, 3L, and 4L) in the spectrum. The MW of these
peaks approximately corresponds to 2, 3 and 4 times that of the 1L peak. Since the RI
signal is proportional to concentration, by integrating the area under the RI traces, the
ratio of high MW rubber and low MW constituents can be obtained. The low MW
fraction was found to constitute ~50% of the toluene-soluble fraction. Table 4.1.1 lists the
MW data. Peak 1H is the average MW data given from the MALLS detector while peaks
1L~4L are peak MW data calculated from a MW-elution time calibration curve
extrapolated from log MW-log elution time graph. Low molecular weight (4,000 Da) NR
was observed earlier by Archer et al. and Asawatreatanakul et al.3,8 Our high resolution
SEC analysis is of particular interest in our pursuit to understand natural rubber biosynthesis because of the identification of a high fraction of low MW intermediates.
Figure 4.1.4 – SEC RI trace of WRP-1.
75 Table 4.1.1 – HR-SEC data of WRP-1. a a b b b b 1H Mw/Mn 1H 1L 2L 3L 4L
(g/mol) Rg (nm) (g/mol) (g/mol) (g/mol) (g/mol)
WRP-1 1.63x106 2.12 80.5 500 900 1,600 2,400 a determined from MALLS detector. b determined from MW-elution time calibration curve.
Figure 4.1.5 presents the conformation plot (log Rg vs log Mn) for the high MW region of the toluene-soluble fraction isolated from WRP-1. From the plot, the slope of
0.539 suggests that this is a linear polymer. NR is known to have long-chain branched molecules. Field-Flow Fractionation (FFF) Chromatography of NR with 50% gel content showed long chain branching/gel (slope of 0.3~0.4).5
Figure 4.1.5 – Conformation Plot of WRP-1.
With enzymatically active WRP-1 from RRIM600, several in vitro experiments were conducted at the USDA under conditions that mimic the in vivo environment of the
76 cytosol. More specifically, the FPP initiator and the IPP monomer were incubated with
WRP-1, which contained the membrane-bound cis-prenyl transferase enzyme in buffer solution. The in vitro reactions were terminated after 5 and 24 hours by the addition of
Ethylene-Diamine-Tetraacetic-Acid (EDTA). EDTA is a ligand that strongly chelates with metal co-factors (Mg2+ or Mn2+). The presence of free co-factors to coordinate with the pyrophosphate end-groups is necessary for the activation of the dormant chain-end
and the polymerization.
Figure 4.1.6 compares the RI traces of representative 5 and 24 hour-incubated
samples with WRP-1. The 1H peak of WRP-1/24 shifted to higher molecular weight
relative to WRP-1 and WRP-1/5, and a distinctive second peak (2H) appeared with an
approximate MW of ~5×105 g/mol (Figure 4.1.6b). This observation is similar to the SEC traces reported in the literature when radio-labeled 14C-IPP monomer3 was used. For this
particular experiment, the weight fraction of the high MW materials (from integration of
the RI signals) increased to ~80% from 50% in the WRP-1. The evidence of MW growth
is supported by the increase of Rg and the increase of the high MW mass fraction. The Rg increased from 80.5 nm of the WRP-1 to 93 nm in WRP-1/24. Therefore, the 2H peak was identified to be newly-formed NR.
77 b) a) 1.2 1H WRP-1 1.0 WRP-1 WRP-1/5 1H 1.0 WRP-1/5 WRP-1/24 0.8 WRP-1/24 0.8
0.6 0.6 2H 2H 0.4
Relative scale 0.4 Relative scale 0.2 0.2
0.0 0.0
5 6 7 105 106 107 10 10 10 Molecular Weight (g/mol) Molecular Weight (g/mol)
Figure 4.1.6 – SEC of WRP-1, WRP-1/5 and WRP-1/24. High MW region. a) LS trace, b) RI trace.
The low MW fractions of the in vitro rubbers also show interesting changes.
Peaks 1L, 2L and 3L diminished with the rise of a new low MW peak, 5L, shown in
Figure 4.1.7. The peak MWs for the well-resolved low fractions are shown in Table 4.1.2.
1.2 WRP-1 2L WRP-1/24 1.0
0.8
0.6 4L 5L Relative scale 0.4 1L 3L 0.2
0.0 103 104 Molecular Weight (g/mol)
Figure 4.1.7 – SEC RI trace of WRP-1 and WRP-1/24. Low MW region. 78 The MW of 2L is ~900 g/mol, while peaks 4L and 5L correspond to 2,200 and 3,500
g/mol.
Table 4.1.2 – Approximate MW of peaks 1L to 5L from HR-SEC. 1L 2L 3L 4L 5L Sample ID (g/mol) (g/mol) (g/mol) (g/mol) (g/mol)
WRP-1 500 900 1,600 2,400 -
WRP-1/5 400 900 - 2,100 3,300
WRP-1/24 400 900 - 2,100 3,200 b determined from MW-elution time calibration curve.
NR latex from Hevea (H600 clone) was fractionated and the low MW fractions (<
4000 Da) were analyzed by MALDI-ToF MS. Figure 4.1.8 presents the MALDI-ToF
mass spectrum. The presence of AgTFA salt led to the formation of singly charged ions
(Ag+ charge) in the rage of 500-3000 Da. (approximately materials from L4 and L5 from
the HR-SEC.) The mass difference between the peaks was found to be 68 Da,
corresponding to the molecular weight of one polyisoprene repeat unit. From Figure
4.1.8, two distributions of oligoisoprenes can be observed.
79
Figure 4.1.8 – MALDI-ToF spectrum of fractionated low MW Hevea NR. (H600 clone).
Based on the m/z values of the [M+Ag]+ ions observed, the major distribution has
end groups of 32 Da, whereas the minor distribution has end groups of 88 Da. The
identification of the structure of these end groups is in progress. Possible end groups with
a mass of 32 Da are CH3OH. Possible end groups with a mass of 88 Da are
(CH3)2CHCH2CH2OH.
In addition to monitoring the growth of NR by HR-SEC, we also wanted to
perform gravimetric analysis. In order to do that, we needed to produce in vitro NR at a
‘larger’ scale. 76 mg WRP-3 from RRIM600 (isolated on a different day than WRP-1)
was incubated with synthetic IPP and FPP in a small centrifuge tube for gravimetric
80 analysis. After 24 hours the final material was freeze-dried to constant weight. The blank was also dried. Table 4.1.3 shows the gravimetric results. Under the conditions used
(shown under Table 4.1.3), substantial mass gain was observed in the sample incubated with IPP and FPP, relative to the blank. The mass gain is more than the IP equivalent of the IPP. However, it should be noted that the experimental error can be high because of the small scale.
Table 4.1.3 – Gravimetric analysis of WRP-3/24. Initial WRP Final Rubber Mass Gain Sample ID (mg) (mg) (mg) KC_030209_WRP (Blank) 76 52 WRP-3/24 104 52 3.8 mL of buffer, 76 mg of WRP + 112 mg IPP (32 mg IP equivalent) + 22 mg FPP (6 mg IP equivalent)
After 24 hours incubation with FPP and IPP, the gel content measured by dialysis reduced slightly from 33wt% to 28wt% (Table 4.1.4). This finding also supported the presence of newly formed soluble in vitro NR.
Table 4.1.4 – Gel fraction analysis of WRP-3 and WRP-3/24. Gel fraction Sample ID (%) WRP-3 33 WRP-3/24 28
The SEC traces and data are presented in Figure 4.1.9 and Table 4.1.5, respectively. In the high MW region, a slight shift of the peak towards higher MW can be seen, but 2H was not observed in this experiment. The Rg after incubation increased and
81 the relative amount of the high MW fraction decreased. Similarly to WRP-1 (Figure
4.1.5), the conformation plot had a slope of 0.54, characteristic of linear polymers.
a) b) WRP-3 0.30 1.2 WRP-3/24 WRP-3 WRP-3/24 4L 0.25 1.0 1H 0.20 0.8 0.15 0.6
Relative scale 0.10
Relative scale 0.4 2L 0.05 0.2
0.0 0.00 5 6 7 103 104 10 10 10 Molecular Weight (g/mol) Molecular Weight (g/mol)
Figure 4.1.9 – SEC traces of WRP-3 before and after incubation. (a) RI traces of low MW region, (b) RI traces of high MW region.
Table 4.1.5 - SEC data of WRP-3 and WRP-3/24.
1H Peak time 1H Peak MW Rg % Mass of Sample ID 6 High MW (min) (10 g/mol) (nm)
WRP-3 35.09 1.28 90 50 WRP-3/24 34.85 1.71 97 40 The retention time difference relative to the WRP-1 set is due to a system pump upgrade performed between the analyses.
In the low molecular weight region, the disappearance of the lowest MW peak,
2L, at around 1,400 g/mol can be observed. Although our SEC analysis showed that the
low MW regions vary within different batches of WRPs made from the same RRIM600 latex, 2L always decreased and 4L increased in the in vitro experiments for all incubations using WRP-1 and WRP-3. (The individual SEC traces are in Appendix B) It
82 had previously been shown that in-vitro NR biosynthesis was able to extend pre-existing
short-chain NR.8
In summary, NRs synthesized in vitro were analyzed by high resolution SEC. The
soluble rubber had approximately 50% high MW fraction between 105 and 3x106 g/mol, and 50% low molecular weight components with MW between 400 and 4,000 g/mol. In the presence of both FPP initiator and IPP monomer, high-resolution SEC was able to resolve the growth of both high and low MW rubber. Further, the formation of new NR was also indicated by mass balance measurements, which showed a net mass gain.
4.2. Substitution of the Isopentenyl Pyrophosphate (IPP) Monomer with Synthetic
Isoprene (IP)
The IPP monomer is produced from carbohydrates in rubber-producing plants as it was discussed in the Introduction. IP is also produced actively by plants and animals.
When excess IPP is present, the equilibrium shifts toward DMAPP which in turn is converted into IP by the isoprene synthase enzyme. IP is an ideal compound to remove excess IPP via the shifts in the equilibria (see Figure 2.3.4) for its ease of evaporation
(boiling point of IP = 34 oC).137 In addition, it is postulated that IP provides heat
protection for plants.138 Efforts in biological research are actively studying the
fundamental processes involved in the bacterial breakdown of terpenoids.139 Since many of the enzymatic reactions are reversible140, Puskas et al. hypothesized that IPP could be
generated in situ by “flooding” the active NR producing latex with IP, and a US patent
83 application has been filed in this regard. The following experiments were carried out to
investigate this hypothesis in detail.
4.2.1. In vitro NR Biosynthesis in the Presence of Synthetic IP
The WRP-3 described in Chapter 4.1 was incubated with FPP as initiator and IP as monomer. No IPP was present in the incubation experiments. The experimental
conditions are listed in Table 4.2.1 below and gravimetric analysis was performed. Since
IP is volatile and the only reagent added to the system, the mass gained after incubation was considered to arise from IP being converted into solids, presumably PIP.
Table 4.2.1 - Experimental conditions for WRP-3 with IP. Sample FPP IPP IP Rxn time (hr) KC_030209_ + - + 24 WRP-3/24(IP) (15μM) (100mM) *3.8 mL of buffer, 76 mg of WRP + 26 mg IP + 22 mg FPP 100 mmol 1L 68.12 g Wt. of IP = 3.8mL 25.9mg L 1000 mL mol
In this experiment, the weight of the IP incubated was calculated as 26 mg as seen
in the footnote of Table 4.2.1. Therefore, the mass gain of in vitro NR biosynthesis can be
used to approximate the conversion of IP into PIP. The weight of the rubber reported
was determined by the mass obtained after drying the samples in the vacuum oven over
five days till constant weight.
84 Table 4.2.2 – Gravimetric analysis summary for experiments with WRP-3. Sample Initial Rubber Wt. diff Conversion WRP (mg) Wt. (mg) (mg) (%) KC_030209_WRP (Blank) 76 52 KC_030209_WRP-3/24(IPP) 52 104 +52 88 KC_030209_WRP-3/24(IP) 52 103 +51 100 (196)
From Table 4.2.2, it was observed that there was a positive mass difference between initial and final polymer weight; suggesting a polymerization reaction has taken place. Further, it was observed that KC_030209_WRP-3/24(IPP) had similar mass gain
compared to KC_030209_WRP-3/24(IP), which was incubated with IP as the monomer.
After the observation that WRP-3 isolated from RRIM600 incubated with
synthetic IP in an in vitro NR biosynthesis showed mass gain, the next set of
experiments involved WRP and raw latex from IAC40 Hevea. IAC40 stands for Instituto
Agronômico de Campinas clone #40 from São Paulo State, Brazil. This particular
genotype carries high NR yield genes. The reason behind switching the genotype was that
our collaborators at the USDA did not have enough stock of RRIM600 Hevea. The
enzymatic activity of IAC40 WRP was determined by procedures described in Chapter
3.1.2, in which the WRP was incubated with 14C-labeled IPP with and without FPP
initiator. The resulting rubber was then isolated and subject to scintillation spectroscopy
to determine the enzymatic activity by the amount of radioactivity. It is important to add
additional initiator when determining enzymatic activity because it was found that the
omission of initiator typically inhibited the enzymatic activity.112 FPP is chosen as the
initiator in this case because it is one of the most effective initiators for Hevea WRPs116 and it is typical to observe a multiple fold increase in enzymatic activity when FPP is added in the assay. Our collaborators at the USDA used the procedures established by
85 Cornish et al.112 and determined that IAC40 WRP was able to incorporate 12.7 µmol/g of
14C -labeled IPP when incubated with FPP synthetic initiator (Figure 4.2.1). When compared to RRIM600 WRP, which could incorporate 10.3 µmol/g dry rubber / 4 hour at
25oC under the same procedure, IAC40 WRP was found to be slightly more reactive.
Figure 4.2.1 – Enzyme activity measurement using 14C-labelled IPP (USDA).
In order to analyze the samples by gravimetric analysis, the solids contents of the starting latex and WRP samples were measured by three different methods. Table 4.2.1a and b show solid content data determined by freeze drying the latex and WRP in vials without washing. Six samples, three latexes and three WRPs were dried to constant weight.
Table 4.2.3a and b show the data for 6 samples (3 IAC40 latex and 3 WRPs) washed three times with buffer (100mM tris-HCl, pH = 7.5) and DI water (distilled, deionized water) after self-coagulation, then freeze-dried to constant weight.
86 Comparison of Tables 4.2.3 and 4.2.4 reveals that ~30% of the solids in the latex and in the WRP were removed by buffer wash. These are most likely non-rubber constituents.
Table 4.2.3a – IAC40 latex solid content determination by freeze drying. Sample Liquid latex Wt. (g) Dried Wt. (g) Solids Content 091409_IAC40_L1 0.5009 0.1289 0.257 091409_IAC40_L2 0.5191 0.1289 0.248 091409_IAC40_L3 0.4981 0.1454 0.292 Average 0.266 Std Dev 0.023
Table 4.2.3b – IAC40 WRP solid content determination by freeze drying. Liquid WRP Wt. Sample (g) Dried Wt. (g) Solids Content 091609_IAC40_W1 0.5091 0.1222 0.240 091609_IAC40_W2 0.5111 0.1201 0.235 091609_IAC40_W3 0.5008 0.1217 0.243 Average 0.239 Std Dev 0.004
Table 4.2.4a – Solids content of IAC40 latex after washing the coagulated rubber. Sample Liquid latex Wt. (g) Washed/Dried Wt. (g) Solids Content 102709_IAC40_L1 0.5101 0.0986 0.193 102709_IAC40_L2 0.5019 0.0937 0.187 102709_IAC40_L3 0.4971 0.0955 0.192 Average 0.191 Std Dev 0.004
Table 4.2.4b – Solids content of IAC40 WRP after washing the coagulated rubber. Liquid WRP Wt. Sample (g) Washed/Dried Wt. (g) Solids Content 120909_IAC40_W1 0.5018 0.0898 0.179 120909_IAC40_W2 0.4997 0.0871 0.174 120909_IAC40_W3 0.5098 0.0916 0.180 Average 0.178 Std Dev 0.003
87 Table 4.2.5a and b show the solids content determined by precipitating the NR
latex and WRP into chilled methanol. Six vials of IAC 40 latex/WRP assays (three each),
were thawed to room temperature and directly precipitated into chilled methanol (4 oC).
The precipitated polymer was white. The polymer was then washed with buffer (100mM tris-HCl, pH = 7.5) and DI water to remove water-soluble solids and freeze-dried in the vacuum oven to constant weight.
Table 4.2.5a – Solids content of IAC40 latex obtained by precipitation in methanol. Liquid Latex Precipitated/Washed Sample Solids Content Wt. (g) /Dried Wt. (g) 071910_IAC40_L4 0.4468 0.0852 0.191 071910_IAC40_L5 0.3823 0.0721 0.189 071910_IAC40_L6 0.5482 0.1085 0.198 Average 0.192 Std Dev 0.005
Table 4.2.5b – Solids content of IAC40 WRP obtained by precipitation in methanol. Liquid WRP Wt. Precipitated/Washed Sample Solids Content (g) /Dried Wt. (g) 071710_IAC40_W4 0.6139 0.1023 0.167 071710_IAC40_W5 0.6993 0.1144 0.164 071710_IAC40_W6 0.7760 0.1217 0.157 Average 0.162 Std Dev 0.005
The solids content determined by methanol precipitation followed by buffer wash
are very similar, with the WRP solids being somewhat lower than the latex solids. Based
88 on these data, we considered the rubber content in the latex and in WRP 19 and 17 wt%, respectively. This may be the same within experimental error.
Utilizing the solids contents above, Table 4.2.6 summarizes the in vitro experiments carried out. The initial rubber weight was a calculated value evaluated from the liquid weight of the latex/WRP used multiplied by the solids content. The final dried/washed rubber weight is the final weight of the sample after 24 hours of incubation followed by washing with buffer and freeze-drying till constant weight. The mass difference between the final dried weight and the initial rubber weight is the mass gain, which is also shown as percentage value in Table 4.2.6. The final weight contained both gel and soluble fractions of NR. The sample identification code highlights the date, type of latex/WRP and the variation in the experiment. For instance,
KC_102009_IAC40_W_IP2 (10% EtOH) signified that the experiment was conducted on
10/20/2009 using WRP of IAC40 Hevea. The monomer used was IP and two samples had either 5% or 10% w/w ethanol added into the in vitro biosynthesis. With the exception of these two experiments, the other experiments were also monitored by in situ
Raman spectroscopy that will be discussed in Section 4.3; 80X and 50X refers to the size of the objective used in the Raman experiments. From Table 4.2.6, consistent mass gain was observed with the lowest being KC_111809_W_IP11 at 25%. The low mass gain of
25% from KC_111809_W_IP11 might be a result from loss of enzymatic activity because that particular batch of WRP was not assayed before use. Enzymatic activities are typically lost from repeated thawing and freezing cycles. The latex particles could coagulate when the water in the latex freezes. In all other cases, both the latex and the
WRP yielded 50% to 100% of mass gain.
89 Table 4.2.6 – Summary gravimetric data of in vitro NR samples. Initial Final Mass gain Mass gain Sample Rubber Dried/Washed (g) (%) Wt. (g) Rubber Wt. (g) KC_092909_IAC40_ 0.101 0.177 0.076 75 L_IP3 (80X) KC_092909_IAC40_ 0.098 0.179 0.081 83 L_IP4 (80X) KC_100909_IAC40_ 0.089 0.212 0.123 100(139) L_IP5 (80X) KC_102109_IAC40_ 0.090 0.193 0.103 100 (114) W_IP8 (50X) KC_110509_IAC40_ 0.090 0.134 0.045 50 W_IP9 (50X) KC_111209_IAC40_ 0.090 0.169 0.079 87 W_IP10 (50X) KC_111809_IAC40_ 0.104 0.130 0.026 25 W_IP11 (50X) KC_111909_IAC40_ 0.090 0.152 0.062 69 W_IP12 (50X) KC_101909_IAC40_ 0.090 0.137 0.047 52 W_IP1 (5% EtOH) KC_102009_IAC40_ 0.093 0.135 0.042 45 W_IP2 (10% EtOH)
The gel content was determined by freeze-drying insoluble and soluble portions to
constant weight after dialysis through 0.6 µm PTFE dialysis filter. Table 4.2.7
summarizes the results with the starting materials’ gel content in bold. The rubber
obtained from latex had higher gel content than that obtained from WRPs. This difference
arises from the gel being removed by the repeated centrifuging purification process in case of WRP extraction. From Table 4.2.5, it can be observed that gel content
consistently increased after incubation except for the samples where ethanol was added,
where the gel content remained the same within experimental error. This was expected
90 because ethanol was reported in the literature to break down the hydrogen bonding
present in the “soft” gel of NR.37
Table 4.2.7 – Gel content of in vitro NR samples.
Sample Gel content (%) KC_102709_IAC40_Latex 31.9 KC_092909_IAC40_L_IP3 (80X) 34.7 KC_092909_IAC40_L_IP4 (80X) 33.6 KC_100909_IAC40_L_IP5 (80X) 35.4 KC_120909_IAC40_WRP 23.8 KC_102109_IAC40_W_IP8 (50X) 29.5 KC_110509_IAC40_W_IP9 (50X) 29.2 KC_111209_IAC40_W_IP10 (50X) 32.9 KC_111809_IAC40_W_IP11 (50X) 27.1 KC_111909_IAC40_W_IP12 (50X) 25.9 KC_101909_IAC40_W_IP1 (5% EtOH) 21.8
KC_102009_IAC40_W_IP2 (10% EtOH) 23.0
Figure 4.2.2 shows the comparison between the SEC traces of the soluble
fractions obtained from IAC40 latex and IAC40 WRP. Figure 4.2.2 presents the zoomed
RI traces of the high and low MW regions for closer comparison. WRP has a shoulder
(H2*) at ~105 g/mol in the high MW region next to the main peak (H1) at ~106 g/mol.
This shoulder was not observed in the latex. In the low MW region, the WRP does not have L2, and the L3 peak is more pronounced in the WRP compared to latex.
91
Figure 4.2.2 – Zoomed SEC RI chromatograms of the soluble fractions from IAC40 and WRP for comparison: a) high MW region, b) low MW region.
The SEC traces show a substantial amount of low MW (< 4000 g/mol) fractions in both samples (Table 4.2.8). We have observed this in all samples we have analyzed.
The relative amounts were determined by the comparison of the RI traces, which are proportional to concentration. The SEC analysis shows that the soluble fraction obtained from WRP had slightly lower high MW components compared to the latex (24% vs
27%). Also, it was observed that all of the latex samples demonstrated an increase in the amount of high MW fraction with incubation of IP. The most pronounced was
KC_100909_L_IP5, in which the high MW fraction grew to 34% from the 27% of the latex. In the soluble fraction of the WRP samples, the high MW fraction also increased, but not as pronounced as in the latex examples. It should be noted here that the gel content also increased after incubation with IP in each case.
92 Table 4.2.8 – High and low MW parts of the soluble fractions obtained from the IAC40 latex and WRP. High MW fraction Low MW Sample (%) fraction (%) KC_102709_IAC40_Latex 27% 73% KC_092909_IAC40_L_IP3 (80X) 31% 69% KC_092909_IAC40_L_IP4 (80X) 30% 70% KC_100909_IAC40_L_IP5 (80X) 34% 66% KC_120909_IAC40_WRP 24% 76% KC_102109_IAC40_W_IP8 (50X) 25% 75% KC_110509_IAC40_W_IP9 (50X) 26% 74% KC_111209_IAC40_W_IP10 (50X) 24% 76% KC_111809_IAC40_W_IP11 (50X) 27% 73% KC_111909_IAC40_W_IP12 (50X) 29% 71% KC_101909_IAC40_W_IP1 (5% EtOH) 27% 73% KC_102009_IAC40_W_IP2 (10% EtOH) 29% 71%
Tables 4.2.9a and 4.2.9b summarize the SEC data. The H1 and H2 peak molecular weights were computed from the light scattering traces by ASTRA V. The H1 peak did not grow to higher MW after incubation with IP. In the soluble fraction obtained from the latex, a new peak appeared at ~ 105 g/mol, which was labeled as H2. Figure 4.2.3 shows the SEC RI trace of KC_092309_L_IP1 compared to the starting latex
(KC_102709_IAC40_Latex). All the latex samples show this new peak. However, in the case of the WRP samples, H2 overlaps with H2* (a shoulder peak in the starting WRP) and does not show a marked difference.
93
Figure 4.2.3 - SEC RI trace of KC_092309_L_IP1 and starting latex.
In the low MW region (not shown), the L3 and L4 peak intensities became more
pronounced after incubation with IP while the intensity of L1 decreased slightly
compared to the starting latex. (Similar behavior was observed for WRP samples.) L1
had a MW of approximately 400 g/mol while L3 and L4 had MWs of ~1,200 g/mol and
~2,000 g/mol respectively, using PIP calibration. Interestingly, the addition of EtOH introduced a new low MW peak labeled as L1*, which had a MW of ~200 g/mol. It is important to note that L1 always have the highest intensity after incubation with IP. ESI showed that L1was mostly composed of phospholipids, which were not involved in the in vitro NR biosynthesis.
94
95 H1 and H2 were integrated separately using Galactic GRAMS v5, a software
package that is able to deconvolute overlapping peaks and integrate the areas under the
respective curves in order to obtain the relative amounts based on the RI traces. It is
important to note that the Schultz-Zimm distribution is typically observed for
macromolecules; however, the software package only contains Gaussian fit, which was
used for this analysis. A modified built-in macro was used to fit Gaussian curves under
H1 and H2 peaks of high MW region of each SEC trace. The built-in macro used the least
square method; the modified macro applied the least absolute residual method, which was less sensitive to outliers (in this case, the H1 peak that overlaps with H2 peak, which skewed the least square fit to be broader, light green curve). (Figure 4.2.4)
Figure 4.2.4 - Difference between a) least square fit (unmodified) and b) least absolute residual fit (modified).
Figure 4.2.4 shows the difference between the least square fitting method and the least absolute residual method for KC_092309_L_IP1 as the two peaks are easily identified. It could be seen that the modified code fits better to the actual curve. It was important to note that the difference may seem very little in this example but was 96 significant in some other examples when a very broad H2 peak was present. The relative amounts were calculated as integral H2 / integral H1. Table 4.2.10 shows the summary.
When compared to gravimetric analysis, this data showed less NR growth. This is because this calculation considered the area of H2 as the new rubber. Furthermore, gravimetric analysis also included gel fractions while SEC data only analyzed soluble fractions. In short, although SEC showed less comparative growth than gravimetric analysis, the data was consistent and confirmed the new rubber growth as demonstrated by gravimetric analysis.
The 1H NMR spectrum of KC_092309_IAC40_L_IP1 in the regions of 0-3.5 ppm and 3.75-7.5 ppm are presented in Figures 4.2.5 and 4.2.6, respectively.
KC_092309_L_IP1 is a latex incubated with IP that showed 64% mass gain by gravimetric analysis and 100% growth by SEC. From Figure 4.2.5, it can be observed that the microstructure of NR is cis-1,4 polyisoprene.141 A small peak at 1.63 ppm might correspond to the trans initiator units as described in literature.41 The small signal at 0.9 ppm might indicate some cyclization.136
97
Figure 4.2.5 - 1H NMR (500 MHz) spectrum of KC_092309_L_IP1: 0-3.5 ppm region. (Concentration: 10 mg/mL, 128 scans, d1 = 10 sec, Pulse angle = 90o, T = 25oC, Solvent: toluene-D8.)
Figure 4.2.6 - 1H NMR (500 MHz) spectrum of KC_092309_L_IP1: 3.75-7.5 ppm region. (Concentration: 10 mg/mL, 128 scans, d1 = 10 sec, Pulse angle = 45o, T = 25oC, Solvent: toluene-D8.)
The broad peak of 5.69 ppm shown in Figure 4.2.9 above indicates 1,4-PIP chain enchainment (cis or trans conformation). The 3,4-enchainment was not observed since no 98 peaks could be observed at 4.4 to 4.8 ppm. The CH2=CH- proton of the vinyl group in
1,2-enchainment expected at 6.1 ppm was also not observed. The peaks obtained within
3.99 to 4.18 ppm might have arisen from alcohol or esters groups or from other
“abnormal” functional groups, which was previously reported to be present in NR.142
The 13C NMR spectrum of KC_092309_IAC40_L_IP1 in the regions of 0-50 ppm and 100-150 ppm are presented in Figures 4.2.7 and 4.2.8, respectively. In Figure 4.2.7, the characteristic peaks of trans-1,4 PIP at 16.0 ppm and at 26.9 ppm are not observed.143
In addition, the absence of peaks at 43.1 ppm and 40.4 ppm eliminates the 3,4-144 and
1,2-PIP145 microstructures, respectively. From Figure 4.2.8, the two peaks observed at
125.0 and 135.2 ppm correspond to cis-1,4 PIP.143 The characteristic peaks from other microstructures except cis-1,4 PIP are not observed, which is an indication that our in vitro NR is exclusively cis-1,4 PIP.
Figure 4.2.7 - 13C NMR (125 MHz) spectrum of KC_092309_L_IP1: 0-50 ppm region. (Concentration: 20 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D).
99
Figure 4.2.8 - 13C NMR (125 MHz) spectrum of KC_092309_L_IP1: 100-150 ppm region. (Concentration: 20 mg/mL, 10,000 scans, d1 = 10s, Pulse Angle = 90o, T = 25°C, Solvent: chloroform-D).
Figures 4.2.9 and 4.2.10 show the 13C NMR spectrum of KC_100909_L_IP5 in the 0-50 and 100-155 ppm regions, respectively. The peaks are better defined in this
spectrum because the NMR solvent was switched to benzene-D6; a study from Chen et
al.146 demonstrated that the separation between cis and trans signals of 1,4 polyisoprenes are the greatest in benzene-D6. The mass gain in this sample was 100% and the SEC
showed a ~60% growth of new NR. A 60-100% mass gain suggests that the new rubber
weight constitutes ~35-50% of the total mass of the sample. If the microstructure of the
newly formed rubber were other than that of cis-1,4 PIP, 13C NMR would be sensitive
enough to distinguish the other microstructures that may form during the incubation with
IP. In addition, if the polymerization mechanism were through free-radical or anionic
pathways, we should observe trans-1,4-, 3,4- and 1,2-PIP microstructures.143-145
100
Figure 4.2.9 - 13C NMR (125 MHz) spectrum of KC_100909_L_IP5: 0-50 ppm region. (Concentration: 50 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6).
Figure 4.2.10 - 13C NMR (125 MHz) spectrum of KC_100909_L_IP5: 100-155 ppm region. (Concentration: 50 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6).
101 The 13C NMR spectra of KC_102109_IAC40_W_IP8 are shown in Figures 4.2.11 and 4.2.12. This WRP sample had a mass gain of 100% and SEC growth of 50%. From the two spectra, only peaks corresponding to cis-1,4 PIP enchainment were observed, similar to in vitro samples that used raw IAC40 latex. In fact, all the samples had identical NMR spectra that only showed cis-1,4 PIP enchainment (attached in the
Appendix).
Figure 4.2.11 - 13C NMR (125 MHz) spectrum of KC_102109_W_IP8: 0-50 ppm (500 MHz Concentration: 60 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6).
102
Figure 4.2.12 - 13C NMR (125 MHz) spectrum of KC_102109_W_IP8: 95-155 ppm region. (Concentration: 60 mg/mL, 10,000 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6).
4.2.2. Incubation of Synthetic D-IP with Hevea Latex
In order to obtain spectroscopic evidence of the new rubber formation, deuterated
IP (D-IP) was incubated with IAC40 latex. The D-IP monomer (Source: Oak Ridge
National Laboratory (ORNL), TN, Received: 9/13/2010, Synthesized: 6/3/2008) was
sealed in a vacuumed ampule and claimed to be stable by ORNL. The purity of the
sample was determined prior to use. Figures 4.2.13 and 4.2.14 show the 1H NMR and
13C NMR spectra of IP (99%, Source: Sigma Aldrich) and D-IP obtained from ORNL, respectively. The synthetic procedure for the D-IP147 produces per-deuterated (i.e. 100%
deuterated) monomer; therefore, only little peaks corresponding to IP should appear in
the 1H NMR. The D-IP and IP NMR samples were prepared at the same concentration 103 and compared in Figure 4.2.13. The 1H NMR spectrum of D-IP (Figure 4.2.13) showed many peaks from unknown impurities and it cannot be confirmed that the compound was pure D-IP. However, it was worth noting that the D-IP and IP had the same characteristic odor.
Figure 4.2.13 - Comparison of 1H NMR spectra of IP (red) and D-IP (black). (300 MHz, Concentration: 20 mg/mL, 32 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: chloroform-D).
104 Since 1H NMR spectra cannot distinguish the structure of D-IP obtained from
ORNL, 13C NMR was taken and the comparison spectra are shown in Figure 4.2.14. In the 13C NMR spectrum, several peaks of D-IP resemble that of IP. When a compound is
Figure 4.2.14 - Comparison of the 13C NMR spectra of IP (red) and D-IP (black). (75 MHz, concentration: 20 mg/mL, 32 scans, d1 = 10s, Pulse angle = 90o, T = 25°C, Solvent: benzene-D6).
deuterated, the 13C peak is expected to split into multiple peaks and follow the
multiplicity rule of 2nI + 1, where n is the number of deuteriated nuclei attached to the
reference atom and I is the spin state of the attached deuteriated nuclei. The nuclear spin
of protons (H) is ½ whereas the nuclear spin of deuterium (D) is 1 which means that a 105 single deuterium nucleus can adopt three different spin states: 0, -1 and 1. For example, the 13C-D coupling in the 13C NMR spectrum of chloroform-D shows 2 x 1 x 1 + 1 = 3 multiplets. Since the 13C spectrum of the D-IP in Figure 4.2.17 shows multiple deuterium splitting, this confirmed that the sample obtained from ORNL contains per-deuterated IP with contaminants.
Gas chromatography (GC) data of IP from Sigma-Aldrich and Oak Ridge are shown in Figure 4.2.15. The major peak at 2.5 minutes elution time is assigned to the IP.
The small peak at 4.5 minutes for IP from is assigned to the p-tert-butylcatechol stabilizer. The ratio of the two peaks shows 99.1% purity for Sigmal-Aldrich IP. The D-
IP monomer shows a major peak at 2.5 min elution time as well as three other compounds (elution times: 0.9, 1.8, 3.2 min). Integration of the peaks from GC analysis of D-IP indicates 85.1% purity.
Figure 4.2.15 - GC chromatograms of IP (red) and D-IP (black).
106 The gravimetric results after incubation with D-IP are shown in Table 4.2.10.
(KC092910_L_IP2(50D-IP/50IP) stands for a mixture of 50% D-IP and 50% IP). The initial rubber weight was calculated based on 19.2 wt% solids content in the latex, determined by precipitating the latex into methanol and washing it with buffer. The NR
was freeze-dried till constant weight.
Table 4.2.10 – Gravimetric summary of D-IP experiments. Sample Initial Final Mass diff. Wt. of Wt. of Mass Rubber Dried/ b/w Final D-IP IP gain Wt. (g)* Washed Dried Wt. monomer monomer (%) Rubber and Ini. (g) (g) Wt. (g) Rubber Wt. (g) KC091610_L_ 0.086 0.098 0.012 0.09 0 14.0 IP1(100D-IP) KC091710_L_ 0.091 0.098 0.006 0.10 0 7.2 IP3(100D-IP) KC092910_L_ 0.098 0.122 0.024 0.05 0.05 24.3 IP1(50D-IP/50IP) KC092910_L_ 0.096 0.136 0.040 0.05 0.05 41.6 IP2(50D-IP/50IP) KC092910_L_ 0.097 0.160 0.062 0 0.10 64.1 IP3 (100IP control) KC092910_L_ 0.096 0.150 0.053 0 0.10 55.6 IP4 (100IP control) *based on 19.2 wt% rubber content
The experiments with 100% D-IP yielded 14.0% and 7.2% mass gain. In the experiments where 50/50 mixture of D-IP and IP were employed, more mass gains were observed (i.e. 24.3% and 41.6%). The control experiments (i.e. 100% IP) showed 64.1
and 55.6% mass gain.
107 Figure 4.2.16 shows the 13C NMR spectra of the experiments with 100% D-IP,
50/50 mixture of D-IP/IP and 100% IP in the 0-140 ppm and 20-35 ppm regions,
respectively. We observed the characteristic peaks of exclusively cis-1,4 PIP
microstructure in all samples. There was no peak splitting in any of the samples that
contained D-IP (the D-IP monomer displayed ~15 Hz, or 3~4 ppm peak splitting).
However, in the experiment with 100% D-IP, a new peak appeared at 30.55 ppm.
Currently, we are not able to identify this signal. It was also possible that the
contamination in the D-IP (i.e. 85.1% purity) terminated the active rubber chain ends in
the latex.
Figure 4.2.16 - 13C NMR spectra (125 MHz) of the D-IP experimental series, 091610_D- IP_latex 2 (top), 092910_L_IP1_50D-IP_50IP (middle) and 092910_L_100IP (bottom), o 0-140 ppm region. 10,000 scans, d1 = 10s, Pulse angle = 90 , Solvent: benzene-D6, Sample (concentration: 15 mg/mL for KC091610_L_IP1(100D-IP) and 50 mg/mL for both KC092910 experiments.)
Latex and WRP were also incubated with 13C labeled IP. The NMR spectra showed no
13C signals in the rubber.
In summary, the addition of synthetic IP to in vitro NR biosynthesis increased the
solids content in WRPs and latex, without incorporating into the rubber.
108 4.2.3. In Vitro NR Biosynthesis under CO2 Atmosphere
In plants, the mitochondrial metabolism is controlled by the synthesis of adenosine triphosphate (ATP). A process called tricarboxylic acid (TCA) cycle, which releases carbon dioxide is a fundamental component of the ATP synthesis.82 Therefore, the atmosphere within the plant medium, i.e. cytosol, is enriched by dissolved CO2. In order to closely mimic the environment where NR biosynthesis occurs in vivo, we have developed a series of experiments where the closed system consists of only CO2 atmosphere. (Chapter 3.2.2.4: Figure 3.2.3)
Under CO2 atmosphere, the reaction mixture of WRP and isoprene monomer had a slightly yellower tint compared to experiments conducted under ambient condition.
Please note that “ambient condition” refers to normal atmospheric conditions, where the vials were not purged with carbon dioxide or any other gas.
The gravimetric analysis and gel content determination of four CO2 experiments are presented in Table 4.2.11 and Table 4.2.12, respectively (the Raman monitoring of these experiments will be discussed in Section 4.3). Note that the initial rubber weight was taken based on the 19.2 % solid (i.e. rubber) content in the latex. All the WRP experiments showed significant mass gain, with KC121409_W_IP3 (CO2/50X) showing the highest mass gain at 98%. The gel content of the reaction performed utilizing IAC40
WRP under carbon dioxide atmosphere was measured only for one sample, which did not seem to change after incubation. This is different than what we have previously observed under normal atmospheric conditions, where the gel content was found to increase after
109 incubation. For the experiment conducted with IAC40 latex, it was found that there was minimal mass gain (i.e. 7%) and the gel content remained unchanged.
Table 4.2.11 - Gravimetric analysis of in vitro NR biosynthesis under CO2 atmosphere. Mass diff. Final b/w Final IP Initial Mass Latex/WRP Dried/Washed Dried Wt. Sample monomer Rubber gain Wt. (g) Rubber Wt. and Ini. Wt. (g) Wt. (g) (%) (g) Rubber Wt. (g) KC_120809_L_I 0.6406* 0.130 0.123 0.131 0.008 7 IP1 (CO2/50X) KC_121109_W_ 0.4697 0.100 0.090 0.136 0.046 51 IP1 (CO2/50X) KC_121109_W_ 0.6715* 0.133 0.129 0.208 0.079 61 IP2 (CO2/50X) KC_121409_W_ 0.5085 0.102 0.096 0.190 0.094 98 IP3 (CO2/50X) *Latex/WRP weight for KC_120809_L_IP1(CO2/50X) and KC_121109_W_IP2 (CO2/50X) are higher than the other two samples due to Raman measurement configurational needs, as described in the experimental section.
Table 4.2.12 - Gel content of in vitro NR samples. Sample Gel content (%) KC_102709_IAC40_Latex 31.9
KC_120809_IAC40_L_IP1(CO2/50X) 32.4 KC_120909_IAC40_WRP 23.8
KC_121109_IAC40_W_IP1(CO2/50X) -*
KC_121109_IAC40_W_IP2(CO2/50X) -*
KC_121409_IAC40_W_IP13(CO2/50X) 23.3 *not available
However, despite minimal mass gain after the incubation, the SEC trace, shown in
Figure 4.2.17 shows the appearance of a peak at ~105 g/mol, which we have assigned to the formation of new rubber. Figure 4.2.18 shows an example of IP incubation with
110 WRP. In the low MW region, while no change was observed for the experiment
conducted with latex (i.e. KC120809_L_IP1(CO2/50X), a new peak L2 was observed for
the experiment conducted with WRP (KC121409_L_IP3(CO2/50X). The SEC data are
summarized in Table 4.2.13.
Figure 4.2.17 - SEC comparison RI traces of KC_102709_Latex_IAC40 and KC_121109_L_IP1(CO2/50X).
Figure 4.2.18 - SEC comparison RI traces of KC120909_IAC40_WRP and KC121409_W_IP3 (CO2/50X).
111 The other traces obtained with WRP (KC_121109_IAC40_W_IP1(CO2/50X and
KC_121109_IAC40_W_IP2(CO2/50X) were similar (not shown).
Table 4.2.13 - SEC analysis of the soluble fractions obtained from IAC40 latex/WRP
before and after incubation with IP in CO2. H1 peak H2 peak H1 H2 L4 L3 L2 L1 Sample ID MW MW (min*) (min*) (min*) (min*) (min*) (min*) (g/mol) (g/mol) 102709_IAC 36.15 1.6x106 - - 55.90 58.08 59.47 61.50 40_latex 120809_IAC 40_L_IP1 36.08 1.6x106 41.35 1.5x105 55.16 57.91 59.02 60.88 (CO2/50X) 120909_IAC 40_WRP 35.93 2.0x106 - - 55.11 58.16 - 61.62 (CO2/50X) 121409_IAC 40_W_IP3 36.21 1.5x106 40.84 4.3x105 55.08 58.53 59.81 62.03 (CO2/50X) *elution time
4.2.4. In Vitro NR Biosynthesis in the Presence of Amylene
Control experiments with the addition of amylene (Figure 4.2.19), an isomer of
IP, were carried out. Of the four reactions, three were repeats of previous experimental
conditions.
Figure 4.2.19 – Chemical structure of amylene.
112 One reaction was monitored by Raman spectroscopy which will be discussed in
Section 4.3. The gravimetric results are summarized in Table 4.2.14. Limited mass gains
were observed in these samples. The SEC for KC_101510_L_Amy1 was prepared by
dissolving the product in benzene and the gel fraction was filtered out using a 0.45 μm
PTFE membrane filter. From Figure 4.2.20 below, the SEC of
KC_101510_L_Amy1showed no changes in the RI trace. No new peaks were
Table 4.2.14 – Gravimetric summary for Amylene experiments. Final Mass diff. b/w Initial Mass Dried/Washed Final Dried Wt. Sample Rubber Wt. gain Rubber Wt. and Ini. Rubber (g) (%) (g) Wt. (g) KC101510_L_Amy1 0.0976 0.1118 0.0142 14.6% KC101510_L_Amy2 0.0961 0.1211 0.0250 26.1% KC101510_L_Amy3 0.0967 0.1114 0.0147 15.1%
Figure 4.2.20 – SEC comparison RI traces of 102709_Latex and KC_101510_L_Amy1 observed after incubation of IAC40 NR latex with amylene. The other two experiments (KC101510_L_Amy2 and KC101510_L_Amy3, not shown) showed similar results with KC101510_L_Amy1 with no changes in the SEC traces. 113 Based on the experiments presented in Section 4.2, we can conclude that the addition of synthetic IP to NR latex and WRP results in net mass gain, but the IP does not incorporate into the rubber. It is very likely that the IP triggers a biological mechanism that releases IPP, leading to new rubber formation.
4.3. In Situ Micro-Raman Monitoring of In Vitro Natural Rubber (NR) Biosynthesis
In order to monitor IP incorporation into NR in situ, a new Raman methodology had to be developed. This was accomplished in collaboration with Professor Sokolov and his Ph. D. student Andrei Malkovskiy in the Department of Polymer Science at the
University of Akron. The method developed is detailed below.
4.3.1. Raman Monitoring using Glass Slides
Spectra were separately obtained for the synthetic high cis-PIP (prepared by anionic polymerization), the IP stabilized by 100 ppm p-tert-butylcatechol (Sigma-
Aldrich) and a WRP (RRIM600, USDA) sample (KC_030209_WRP1). 10 mg of the
WRP sample was placed between two fresh pre-cleaned microscope glass slides
(Fisherbrand® plain microscope slides, 25x75x1 mm) and positioned perpendicular to the incident laser beam (λ = 647 nm) of moderate intensity (~ 1mW). RRIM600 WRP samples taken from a refrigerator a few minutes prior to the measurements, in which the
WRP should be still active, were used in all the measurements. The slides were pressed tightly in a standard spring holder. The spectrum of the sample was measured together
114 with the corresponding background spectra of both the top and the bottom glass slides.
All the data were corrected by subtracting the background glass signals from the spectra of the samples of interest. We found many characteristic peaks of PIP: two peaks at
~1000 and ~1040 cm-1, three broad peaks at ~1320, ~1370 and ~1450 cm-1 and a peak at
~1670 cm-1. However, after a detailed analysis on the combination of spectra, we decided
to focus only on the peak at 1670 cm-1, because of its sharpness along with the highest intensity of absorption. This peak is attributed to the C=C bond of PIP. We have found
this signal in both the synthetic PIP and the RRIM600 WRP. The shoulder next to this
peak in the PIP standard remains unidentified at this point. The signal of the conjugated double bond in IP appeared at 1640 cm-1 (see Figure 4.3.1).
Figure 4.3.1 - Signals attributed to the C=C Raman-active vibrations in PIP and IP (Isoprene: liquid IP with stabilizer; Mixed sample: WRP RRIM600+IP 2/1 (w/w)).
115 The difference in the vibrational energy for the IP and PIP peaks is less than 30
cm-1, which was easy to resolve with Sokolov’s Raman system. Figure 4.3.1 also shows
the signal of the sample marked “mixed” in which IP was added to the RRIM600 WRP
(2:1 w/w WRP:IP) and allowed to react for ~5 minutes. In this case, the spectrum of the
bottom glass slide was not measured because the sample was opaque. Six different
spectra were measured for the mixed sample: 2 spectra from random spots, 3 spectra
from different WRP particles and 1 spectrum from the last latex particle exposed to five
minutes of laser illumination (to observe whether there was sample damage from the
laser). In the mixed sample, the signals of both IP and PIP were detected, with the PIP signal being less intense.
4.3.2. Raman Monitoring with Micro-cavity Slides.
IP has a boiling point 34 oC and easily evaporates at room temperature. To avoid
IP evaporation between two glass slides, special glass slides (Pearl®, clear glass with ground edges, 25.4x76.2 mm, ~1.1 mm thick) with a small cavity have been purchased.
The top slide was Pearl® cover glass slides (~0.15 mm thickness). The bottom slide had a cavity, which allowed higher volumes of material to be placed on the slide, while at the same time ensuring a better seal of the two-slide assembly to avoid IP evaporation. The latex invariably adhered to the outer edge of the cavity when sealed due to strong capillary forces. This made signal acquisition possible even when the cavity was only partially filled and limited the evaporation of IP. The Raman system also allowed video- monitoring of the sample under the microscope. It enabled observation of the probed
116 volume and the exact spot illuminated by the laser. An external white lamp was
connected to the microscope to provide a more homogeneous illumination source. With
the help of this camera, another observation was made: the spectra measured at the
position of a single latex particle were generally much stronger than those measured
away from any particles, while the fluorescence background from the bottom glass slide
was also weaker. This probably indicates that the observed Raman signal comes mostly
from the particles and not from the surrounding media. Despite much better sealing of the
sample between the glass slides with a cavity, IP evaporation could not be excluded.
4.3.3. Raman Monitoring in Sealed Silanized Vials
It is crucial to develop Raman experiments methodologies where we can be sure that no IP is lost due to evaporation. 0.5 mL IAC40 WRP and IAC 40 latex samples were sealed in glass vials (Fischer Scientific, 1ml silanized glass vials) using a crimper. After the injection of IP (0.102g, 0.15mL, 1.50mmol) through the hermetic cap of the crimp, the contents of every vial were vigorously shaken for a minute to ensure good mixing of the IP and the initial rubber particles. Then the bottle was fixed under a long-working distance Mitutoyo APO SL50 objective (50X, NA = 0.42) in horizontal position.
Photographs of the setup are shown in Chapter 3.2.2.3 (Figure 3.2.2). Measurements were also performed with 20X and 80X (NA = 0.42) Mitutoyo long-working distance objectives as well. However, the 20X objective was collecting significant extra Raman signals from the glass walls of the vial (due to larger focal volume of the objective). The
80X objective gave much lower overall signal intensity, when compared to the 50X 117 objective. After comparing the data measured with the three objectives described above, the 50X objective was chosen as the one providing the best Raman signal of IP and PIP with very low glass background signal. The Raman signals were measured immediately after the IP injection and mixing (about 1 minute) through the glass walls. The spectra were collected for five minutes for every data point with intervals of five minutes between the measurements for the duration of the first six hours of the experiment. Then the samples were incubated for 18 more hours for a total incubation time of 24 hours.
Figure 4.3.2 shows the positioning of the laser beam. It probes an area of ~1 cubic micron, which is roughly the size of an average particle and very localized. The
RRIM600 average particle size is approximately 1.1±0.6 μm and the IAC40 average particle size is approximately 1.6±0.5 μm. This makes the quantification of the Raman data difficult.
Figure 4.3.2 - The schematics of the bottle illuminated by the Raman beam.
Another challenge was the strong fluorescence. Continuous illumination of a single spot raised the fluorescence of the sample to a degree that the experiment could not be continued. A different spot had to be picked and re-focused, which makes quantitative 118 analysis impossible. This problem is illustrated in the Figure 4.3.3 for an IAC40 latex
sample; however the fluorescence problem also persisted for the WRP samples. We speculated that one reason contributing to the scattering of data points might be the 80X objective, which focuses on a small area of the rubber particles. Therefore, we decided to enlarge the probing area by switching to a 50X objective and also by blocking the beam between collections, which was applied in all subsequent experiments.
Figure 4.3.3 - Fluorescence problems illustrated for KC_092309_L_IP1 with 80X objective. (092309_L_WRP: 0.5340g IAC40 latex, 0.1022g IP, 24h, RT).
Figure 4.3.4 presents a set of Raman spectra of an experiment with IAC40 WRP
(KC_102109_W_IP8 (50X)) as a function of time, where the IP and PIP Raman signals are marked. It is apparent that the IP peak intensity decreases while the PIP signal intensity increases. The experiment was repeated twice. For more quantitative analysis, the spectra in the frequency range of interest were fitted by two Lorentzian peaks, one for the IP signal at 1640 cm-1 and another for PIP signal at 1670 cm-1 (Figure 4.3.4).
119
Figure 4.3.4 - Raw spectra for a sequence of data points of KC_102109_W_IP8 (KC_102309_WRP_IP8: 10 min between each spectra, 0.5079g IAC40 WRP, 0.1022g IP, 24h, RT).
Due to noise in the spectra, the fit gives fluctuating values of the peak positions
and widths. In order to improve the accuracy of our analysis, we calculated the average
values of these parameters for each data set. In the next iteration, the spectra were fitted
again with the peak width and position fixed at the averaged values of the set. The areas
under the fit curves were used to estimate the integrated intensity of each signal. The ratio of the PIP peak area to the sum of the IP and PIP peak areas thus is a semi- quantitative illustration of the kinetics of PIP formation. Absolute measurements of the
Raman intensity revealed sometimes strong change of the signal due to the fact that the overall amount of material next to the top wall of the vial (that is placed on its side under the microscope objective) might have changed over time due to gravitational forces, preventing us from plotting just the growth in the PIP peak area.
Figure 4.3.5 presents a comparison of the ( / ) – time plots for two
representative experiments. In both cases, we see a decrease in the early part of the 120 experiment. KC_120209_WRP_IP13 remained constant while KC_110509_WRP_IP9
showed an increase. After extensive experimentation, we realized that this was due to an artifact as a consequence of inadequate mixing. We also observed that PIP formation was seen only when a yellow color appeared in the mixtures. This was the case for
110509_WRP_IP9 (red circles) showing an increasing trend, most likely due to adequate mixing. We believe that the yellow color indicates the presence of ionic species.
120209_WRP_IP13 (green stars) was white (no yellow color appeared upon addition of the IP). The data points are from single measurements over time.
Figure 4.3.5 - Normalized PIP formation plots for two repeat experiments using 50X objective. (KC_110509_WRP_IP9: 0.5028g WRP, 0.1022g IP, 24h, RT. KC_120209_WRP_IP13: 0.5097g WRP, 0.1021g IP, 24h, RT).
Figure 4.3.6 shows PIP formation plots for two samples that changed their color to yellow upon IP addition, observed under the 50X objective, and the beam was blocked in between data acquisition steps. The absence of the initial decrease, as in Figure 4.3.6, 121 was the evidence for good sample mixing. The intensity of the PIP signal doubled in the two samples (102109_W_IP8 and 111209_W_IP10). The size of the error bars showed the reliability of the Lorentzian fits and consistency between the experimental points.
Figure 4.3.6 - Normalized PIP formation plots for two repeat experiments with 50X objective with error bars. (KC_102309_WRP_IP8: 0.5079g WRP, 0.1022g IP, 24h, RT. KC_111209_WRP_IP10: 0.5843g WRP, 0.1022g IP, 24h, RT).
Figure 4.3.7 shows IP/(PIP+IP)–time plots. Qualitatively, the plots demonstrated decreasing trends. The IP signal never disappeared completely. This could be explained by the position of the probed volume. The Raman spot was probing a very small volume, located next to the glass wall of the silanized vial, where IP could get trapped in the confined space.
122
Figure 4.3.7 - Normalized IP consumption plots for three repeat experiments with 50X objective. (103209_WRP_IP8: 0.5079g WRP, 0.1022g IP, 24h, RT. 110509_WRP_IP9: 0.5028g WRP, 0.1022g IP, 24h, RT. 111209_WRP_IP10: 0.5843g WRP, 0.1022g IP, 24h, RT).
Figure 4.3.8 shows the result of in situ Raman monitoring experimental method
that had been optimized after many experiments. The experimental procedure was as
follows: 0.5 g active IAC40 WRP or IAC40 latex were sealed in glass vials (Fischer
Scientific, 1ml silanized glass vials) using a crimper. After the injection of isoprene
(0.102 g, 0.15 mL, 1.50 mmol) through the hermetic cap, the contents were vigorously shaken for one minute to ensure complete mixing. The color of the mixture was observed and noted. The reactions were monitored by in situ Raman spectroscopy to observe PIP growth. The sealed polymerization vial was fixed under a long-working distance 50X objective from Mitutoyo with NA = 0.42. The laser source was Lexel RamanIon Krypton laser and the excitation wavelength was set at 647 nm. Raman signals were collected by a
123 Horiba Jobin-Yvon Labram HR single monochromator equipped with a nitrogen-cooled
CCD camera through the glass walls of the vials. Spectra were collected for five minutes for every data point, and then the laser was blocked for five minutes to avoid heating and fluorescence. This sequence was repeated for the duration of the first six hours of the experiment. The samples were incubated for a total of 24 hours. From Figure 4.3.8, the
Raman plots demonstrate IP decrease and PIP increase using two equations: /