Catalysis 9.1 General Principles of Catalysis Turnover Number: the Average Number of Reactants That a Catalyst Acts on Before the Catalyst Loses Its Activity

Total Page:16

File Type:pdf, Size:1020Kb

Catalysis 9.1 General Principles of Catalysis Turnover Number: the Average Number of Reactants That a Catalyst Acts on Before the Catalyst Loses Its Activity Chapter 9 Catalysis 9.1 General principles of catalysis Turnover number: the average number of reactants that a catalyst acts on before the catalyst loses its activity. The catalyst increases rate of reaction (decreases activation energy). The thermodynamics of a catalyzed reaction are unaffected by the catalyst. A heterogeneous catalyst: one that does not dissolve in the solution. Ex) Pd/C A homogeneous catalyst: one that dissolves in the solution. All calaysts operate by the same general principle – that is, the activation energy of the rds must be lowered in order for a rate enhancement to occur. 9.1.1 Binding the transition state better than the ground state Substrate: any material (reactant) used in a catalytic reaction Activated complex: simply referred to as the transition state Rate enhancement: the ratio of the rate constant for the catalyzed reaction to that for the uncatalyzed one. To achieve catalysis, the catalyst must stabilize the transition state more than it stabilizes the ground state. That is, the transition state must be bound better than the ground state. 1 2 9.1.3 A spatial temporal approach To achieve catalysis, the catalyst must stabilize the transition state more than it stabilizes the ground state. That is, the transition state must be bound better than the ground state. Another explanation for catalysis: spatial temporal postulate, many intramolecular reactions are often much faster than corresponding intermolecular reactions. -> the rate of reaction between functionalities A and B is proportional to the time that A and B reside within a critical distance. The longer that A and B spend together in the correct geometry for reaction, the greater that probability. When bound to the catalyst, the distance between A and B is closer than when they are free in solution, and inherently the transition state brings A and B close because bonds are beginning to form. In summary, binding is the key element in the most widely accepted theory of how catalysis is achieved. Greater binding of the transition state relative to the ground state is all that needs to be invoked to give a rate enhancement. 3 9.2 Forms of catalysis 9.2.2 Proximity as binding phenomenon Intermolecular aminolysis (k1; 1/M·s) 1.3 x 10-4 /M·s Intramolecular cyclization (k2; 1/s) 0.17/s -> a rate enhancement of 1200 Effective molarity (E.M.) or intramolecularity; ratio of the first order to second order rate constants for the analogous reactions. -> tell us the effective concentration of one of the components in the intramolecular reaction 4 Entropies of translation and rotation 5 Gem-dimethyl effect: sterically compress two groups together and preorganize two reactants in proximity close decrease of angle R R 6 Twisted amide 11 12 E.M. = 10 -10 -> very reactive Tetrahedral intermediate -> infinitely stable 7 9.2.3 Electrophilic catalysis Electrophilic catalysis includes simple electrostatics, hydrogen bonding, acid catalysis, and electrophilic metal coordination. Electrostatic interactions Oxyanion hole 8 150-fold rate enhancement Cation-π interactions 9 Metal ion catalysis 2 x 1016-fold rate enhancement pKa of metal-bound water = 7.2 (108 more acidic than water itself) 10 11 9.2.4 Acid-base catalysis; 9.3에서 설명 9.2.5 Nucleophilic catalysis Nucleophilic catalysis arise when a nucleophile binds to a reactant and enhances its rate of reaction. -> less common than electrostatic catalysis better electrophile and more reactive than the starting acid halide or anhydride NMe2 NMe2 N N H DMAP; N,N'-dimethylaminopyridine 12 9.2.6 Covalent catalysis Iminium ion enamine 13 14 9.2.7 Strain and distortion When a substrate binds to a catalyst that is more complementary in structure or electronic characeristics to the transition state, the substrate may distort in order to optimize binding interactions. That is, because the catalyst is designed to optimally bind the transition state, it necessarily is not optimal for the most stable structure of the ground state. -> distortion as a strain on the substrate -> the strain raises the energy of the substrate -> diminish activation energy 15 16 The chair is distorted into a conformation resembling a half-chair 9.3 Brønsted acid-base catalysis 9.3.1 specific catalysis The specific acid is defined as the protonated form of the solvent in which the reaction is being performed. + + + eg) H3O , CH3CNH , CH3SO(H )CH3 The specific base is defined as the conjugate base of the solvent. - - - eg) HO , CH2CN, CH3SOCH2 The specific acid catalysis refers to a process in which the reaction rate depends upon the specific acid, not upon other acids in the solution. The specific base catalysis refers to a process in which the reaction rate depends upon the specific base, not upon other bases in the solution. 17 + kobs = k[H3O ]/KaRH+ Specific acid catalyzed reactions added acid (AcOH in H2O) A-는 반응에 관여하지 않음. 따라서 rate law에 포함되지 않음 - + KaHA = [A ][H3O ]/[HA] + + KaRH+ = [R][H3O ]/[RH ] 앞과 동일 [HA] 항 없음 If the acid catalysis is involved in an equilibrium prior to the rds, and it is not involved in rds, then the kinetics of the reaction will depend solely upon the concentration of the specific acid. This is true even if an added acid (AcOH) is involved in protonating the reactant. Why? When a prior equilibrium is established, [RH+] determines the rate of the reaction. + + The concentration of RH depends solely upon the pH and the pKa of RH , and does not depend upon the concentration of the acid HA that was added to solution. 18 Specific base catalyzed reactions BH+는 반응에 관여하지 않음. 따라서 rate law에 포함되지 않음 - + KaRH =[R ][H3O ]/[RH] + kobs = kKaRH /[H3O ] [B] 항 없음 23 page에서 다시 설명 19 Kinetic plots The hallmark of specific acid or specific base catalysis is that the rate depends on the pH and not on the concentration of various acids or bases. This always means that an equilibrium involving the acid or base occur prior to rds, and the acid or base is not involved in rds itself. specific acid catalysis specific base catalysis k = k[H O+]/K + obs 3 aRH+ kobs = kKaRH /[H3O ] logkobs = logk–pH-logKaRH+ logkobs = logk+pH+logKaRH+ added acid added base 20 9.3.2 General catalysis In case that the proton transfer is involved in rds, not in a prior equilibrium -> general catalysis When an acid is involved in rds, -> general acid catalysis When a base is involved in rds, -> general base catalysis The term ‘general’ refers to the fact that any acid or base we added to the solution will affect the rate of the reaction. The term ‘specific’ refers to the fact that just one acid or base, that from the solvent, affects the rate of the reaction. General acid catalyzed reactions HA는 반응에 관여함. 따라서 rate law에포함 - + Ka = [A ][H3O ]/[HA] + - kobs = k[HA] or k[H3O ][A ]/Ka - Since the acid is always regenerated after the reaction, its concentration never changes over the course of the reaction -> pseudo-first order21 - the concentration of either HA or A- is in the rate expression. General base catalyzed reactions B는 반응에 관여함. 따라서 rate law에포함 - + kobs = k[B] or k[HO ][HB ]/Kb - Since the base is always regenerated after the reaction, its concentration never changes over the course of the reaction -> pseudo-first order - the concentration of either B or BH+ is in the rate expression. 22 19 page slow 실제로는 첫번째 단계가 rds 따라서 HO-는 general base로작용 Note: ‘specific’ is used to designate the protonated or deprotonated form of the solvent + (H3O or HO- for water), but it is also used to designate a mechanism involving an acid or base in an equilibrium prior to rds. However, sometimes hydronium or hydroxide can be involved in rds. In this case the specific acid and base are participating in general-catalysis. 23 Kinetic plots The hallmark of specific acid or specific base catalysis is that the rate depends on the pH and not on the concentration of various acids or bases. This always means that an equilibrium involving the acid or base occur prior to rds, and the acid or base is not involved in rds itself. general acid catalysis general base catalysis + - - + kobs = k[HA] or k[H3O ][A ]/Ka kobs = k[B] or k[HO ][HB ]/Kb 페이지 20과비교 pH < pKa, HA로주로존재, 따라서 k의변화없음 - pH ~ pKa, HA와 A (이것은 반응에 관여하지 않음)이공존 - pH > pKa, HA가 점차적으로 A 로 바뀌어 k가 지속적으로 감소 C와 mirror image general acid catalysis general base catalysis 24 9.3.4 Concerted or sequential general-acid-general-base catalysis Both a general acid and a general base catalyst are required for a reaction. This is often the case with enzymes. acid base kobs = k[HA][B] The rate dependence on pH is a combination of that observed for general-acid and general-base catalyst. The largest kobs is found at pH where the product of the concentrations of HA and B is at a maximum 25 9.4 Enzymatic catalysis physical process 9.4.1 Michaelis-Menten kinetics chemical process k1 kcat E + S ←→ E·S → P + E E·S: Michaelis complex k-1 E + S ←→ → P E·S rate = d[P]/dt = kcat[ES] d[ES]/dt = k1[E][S] – k-1[ES] - kcat[ES] = 0 [E]0 = [E] + [ES] [E] = [E]0 -[ES] k1([E]0-[ES])[S] – k-1[ES] - kcat[ES] = 0 [E] [S] [ES] = 0 Km = (k-1 + kcat)/k1 Km + [S] k [E] [S] cat 0 Michaelis-Menten equation rate = d[P]/dt = kcat[ES] = Km + [S] 26 Kinetic parameters to be determined for enzymatic reactions: kcat and Km 9.4.2 The meaning of Km, kcat and kcat/Km 1.
Recommended publications
  • Physical Organic Chemistry
    CHM 8304 Physical Organic Chemistry Catalysis Outline: General principles of catalysis • see section 9.1 of A&D – principles of catalysis – differential bonding 2 Catalysis 1 CHM 8304 General principles • a catalyst accelerates a reaction without being consumed • the rate of catalysis is given by the turnover number • a reaction may alternatively be “promoted” (accelerated, rather than catalysed) by an additive that is consumed • a heterogeneous catalyst is not dissolved in solution; catalysis typically takes place on its surface • a homogeneous catalyst is dissolved in solution, where catalysis takes place • all catalysis is due to a decrease in the activation barrier, ΔG‡ 3 Catalysts • efficient at low concentrations -5 -4 -5 – e.g. [Enz]cell << 10 M; [Substrates]cell < 10 - 10 M • not consumed during the reaction – e.g. each enzyme molecule can catalyse the transformation of 20 - 36 x 106 molecules of substrate per minute • do not affect the equilibrium of reversible chemical reactions – only accelerate the rate of approach to equilibrium end point • most chemical catalysts operate in extreme reaction conditions while enzymes generally operate under mild conditions (10° - 50 °C, neutral pH) • enzymes are specific to a reaction and to substrates; chemical catalysts are far less selective 4 Catalysis 2 CHM 8304 Catalysis and free energy • catalysis accelerates a reaction by stabilising a TS relative to the ground state ‡ – free energy of activation, ΔG , decreases – rate constant, k, increases • catalysis does not affect the end point
    [Show full text]
  • Aldehydes Can React with Alcohols to Form Hemiacetals
    340 14 . Nucleophilic substitution at C=O with loss of carbonyl oxygen You have, in fact, already met some reactions in which the carbonyl oxygen atom can be lost, but you probably didn’t notice at the time. The equilibrium between an aldehyde or ketone and its hydrate (p. 000) is one such reaction. O HO OH H2O + R1 R2 R1 R2 When the hydrate reverts to starting materials, either of its two oxygen atoms must leave: one OPh came from the water and one from the carbonyl group, so 50% of the time the oxygen atom that belonged to the carbonyl group will be lost. Usually, this is of no consequence, but it can be useful. O For example, in 1968 some chemists studying the reactions that take place inside mass spectrometers needed to label the carbonyl oxygen atom of this ketone with the isotope 18 O. 16 18 By stirring the ‘normal’ O compound with a large excess of isotopically labelled water, H 2 O, for a few hours in the presence of a drop of acid they were able to make the required labelled com- í In Chapter 13 we saw this way of pound. Without the acid catalyst, the exchange is very slow. Acid catalysis speeds the reaction up by making a reaction go faster by raising making the carbonyl group more electrophilic so that equilibrium is reached more quickly. The the energy of the starting material. We 18 also saw that the position of an equilibrium is controlled by mass action— O is in large excess.
    [Show full text]
  • Kinetic and Theoretical Insights Into the Mechanism of Alkanol Dehydration on Solid Brønsted Acid Catalysts
    Article pubs.acs.org/JPCC Kinetic and Theoretical Insights into the Mechanism of Alkanol Dehydration on Solid Brønsted Acid Catalysts William Knaeble and Enrique Iglesia* Department of Chemical and Biomolecular Engineering University of California, Berkeley, California 94720, United States *S Supporting Information ABSTRACT: Elementary steps that mediate ethanol dehydration to alkenes and ethers are determined here from rate and selectivity data on solid acids of diverse acid strength and known structure and free energies derived from density functional theory (DFT). Measured ethene and ether formation rates that differed from those expected from accepted monomolecular and bimolecular routes led to our systematic enumeration of plausible dehydration routes and to a rigorous assessment of their contributions to the products formed. H-bonded monomers, protonated alkanol dimers, and alkoxides are the prevalent bound intermediates at conditions relevant to the practice of dehydration catalysis. We conclude that direct and sequential (alkoxide-mediated) routes contribute to ether formation via SN2-type reactions; alkenes form preferentially from sequential routes via monomolecular and bimolecular syn-E2-type eliminations; and alkoxides form via bimolecular SN2-type substitutions. The prevalence of these elementary steps and their kinetic relevance are consistent with measured kinetic and thermodynamic parameters, which agree with values from DFT-derived free energies and with the effects of acid strength on rates, selectivities, and rate constants; such effects reflect the relative charges in transition states and their relevant precursors. Dehydration turnover rates, but not selectivities, depend on acid strength because transition states are more highly charged than their relevant precursors, but similar in charge for transition states that mediate the competing pathways responsible for selectivity.
    [Show full text]
  • Acid-Base Catalysis Application of Solid Acid-Base Catalysts
    Modern Methods in Heterogeneous Catalysis Research Acid-Base Catalysis Application of Solid Acid-Base Catalysts Annette Trunschke 18 February 2005 Outline 1. Introduction - basic principles 2. Substrates and products 3. Kinds of acid / base catalysts - examples 4. Characterization of surface acidity / basicity - examples 5. Acid catalyzed reactions 6. Base catalyzed reactions 7. Acid-base bifunctional catalysis 8. Summary and outlook Modern Methods in Heterogeneous Catalysis Research : 18/02/2005 2 1. Introduction - Basic definitions concept acid base - + Brønsted H2O OH + H - - Lewis FeCl3 + Cl [FeCl4] Hydrogen transfer reactions intermediates acid-catalyzed + H+ carbenium ions base-catalyzed + H+ carbanions Modern Methods in Heterogeneous Catalysis Research : 18/02/2005 3 1. Introduction - Basic definitions specific acid / base general acid / base catalysis catalysis + - active H3O or OH undissociated acid or base species groups; a variety of species may be simultaneously active reaction •in solution •gas phase reactions medium / •on the surface of •high reaction temperatures conditions a hydrated solid Advantages of solid acid-base catalysts: • Easier separation from the product • Possible reuse and regeneration • Fewer disposal problems • Non-corrosive and environmentally friendly (but not always!) Modern Methods in Heterogeneous Catalysis Research : 18/02/2005 4 2. Substrates and products solid acid catalysis solid base catalysis substrates •Alkanes, aromatics •Alkenes (components of crude •Alkynes petrolium) •Alkyl aromatics •Alkenes (products of •Carbonyl compounds petrolium cracking (FCC, steam cracking)) products •Gasoline components •Chemical intermediates •Chemical intermediates •Fine chemicals •Fine chemicals Industrial processes in 1999: 103 solid acids worldwide production by catalytic cracking: 500x106 tonnes/y 10 solid bases 14 solid acid-base bifunctional catalysts K.Tanabe, W.F.Hölderich, Applied Catalysis A 181 (1999) 399.
    [Show full text]
  • 629 Acid/Base Catalysis 154–157
    629 Index a – – Horvath–Kawazoe (HK) method acid/base catalysis 154–157 525–526 – bimolecular, acid catalyzed reaction 155 – Nonlocal Density Functional Theory – bimolecular, base catalyzed reaction 156 (NL–DFT) 530–532 – Brønsted–Lowry theory 155 – physical adsorption 514–516 – RNA hydrolysis catalyzed by enzyme – theoretical description of adsorption RNase-A 157 519–523 acids 132–143, See also solid acids and bases ––BETtheoryofadsorption 521 Acinetobacter calcoaceticus 181 – – Langmuir isotherm 519–521 activated carbon supports 439 – – standard isotherms 522–523 activation, catalyst 58–64 – – t-method 522–523 – induction periods as catalyst activation – xenon porosimetry 533–534 ® 59–60 Aerosil process 435 active sites 269–273 alcohols activity of catalyst, in homogeneous catalysis – carbonylations of 245–247 54–58 – synthesis 176–177 acylases 185–186, 256 aldolases 190–193 adaptive chemistry methods 370 alkene metathesis 402–406 adiabatic reactor 569 altered surface reactivity 38–39 adsorption entropy 27–30 alumina (Al2O3) and other oxides adsorption methods for porous materials 436–438 characterization 514–534 amidases 185–186 – adsorption isotherms 517–518 amidases catalyzed reactions 256 – application of adsorption methods amino acid dehydrogenases (AADHs) 518–519 177, 253 – Barret–Joyner–Halada (BJH) method amino acids synthesis 177–178 529–530 6-aminopenicillanic acid (6-APA) 256 – classification of porous materials 517 7-aminocephalosporanic acid (7-ACA) 256 – mercury porosimetry 533 ammonia synthesis 114–119, 289–299 – mesoporous
    [Show full text]
  • Factors Affecting the Relative Efficiency of General Acid Catalysis
    Factors Affecting the Relative Efficiency of General Acid Catalysis Eugene E. Kwan Department of Chemistry, University of Toronto, Toronto, Ontario M5S 3H6, Canada* * Now at Department of Chemistry and Chemical Biology, Harvard University, Cambridge, MA 02138, USA Electronic mail: [email protected] Abstract Specific acid catalysis (SAC) and general acid catalysis (GAC) play an important role in many organic reactions. Elucidation of SAC or GAC mechanisms requires an understanding of the factors that affect their relative efficiency. A simple model reaction in which SAC and GAC occur concurrently is analyzed to provide guidelines for such analyses. Simple rules which predict the effect of pH on the relative efficiency of GAC are discussed. An explicit expression for determining the optimal pH at which the effects of GAC are maximized is provided as well as an analogous expression for the general base case. The effects of the pKa of the general acid and the total catalyst concentration on GAC efficiency are described. The guidelines are graphically illustrated using a mixture of theoretical data and literature data on the hydrolysis of di-tert-butyloxymethylbenzene. The relationship between the model and the Brønsted equation is developed to explain the common observation that GAC is most easily observable when the Brønsted coefficient α is near 0.5. The ideas presented enable systematic evaluations of experimental kinetic data to provide quantitative support for SAC or GAC mechanisms. This material is suitable for the curriculum of a senior-level undergraduate course in physical-organic chemistry. Keywords: Organic chemistry; physical chemistry; curriculum; acid-base chemistry; catalysis; kinetics.
    [Show full text]
  • Microwave-Assisted Homogeneous Acid Catalysis and Chemoenzymatic Synthesis of Dialkyl Succinate in a Flow Reactor
    catalysts Article Microwave-Assisted Homogeneous Acid Catalysis and Chemoenzymatic Synthesis of Dialkyl Succinate in a Flow Reactor Laura Daviot 1, Thomas Len 1, Carol Sze Ki Lin 2 and Christophe Len 1,3,* 1 Centre de Recherche de Royallieu, Université de Technologie Compiègne, Sorbonne Universités, Cedex BP20529, F-60205 Compiègne, France; [email protected] (L.D.); [email protected] (T.L.) 2 School of Energy and Environment, City University of Hong Kong, Tat Chee Avenue, Kowloon Tong, Hong Kong, China; [email protected] 3 Institut de Recherche de Chimie Paris, PSL Research University, Chimie ParisTech, CNRS, UMR 8247, Cedex 05, F-75231 Paris, France * Correspondence: [email protected]; Tel.: +33-144-276-752 Received: 12 February 2019; Accepted: 8 March 2019; Published: 16 March 2019 Abstract: Two new continuous flow systems for the production of dialkyl succinates were developed via the esterification of succinic acid, and via the trans-esterification of dimethyl succinate. The first microwave-assisted continuous esterification of succinic acid with H2SO4 as a chemical homogeneous catalyst was successfully achieved via a single pass (ca 320 s) at 65–115 ◦C using a MiniFlow 200ss Sairem Technology. The first continuous trans-esterification of dimethyl succinate with lipase Cal B as an enzymatic catalyst was developed using a Syrris Asia Technology, with an optimal reaction condition of 14 min at 40 ◦C. Dialkyl succinates were produced with the two technologies, but higher productivity was observed for the microwave-assisted continuous esterification using chemical catalysts. The continuous flow trans-esterification demonstrated a number of advantages, but it resulted in lower yield of the target esters.
    [Show full text]
  • Brønsted and Lewis Solid Acid Catalysts in the Valorization of Citronellal
    catalysts Article Brønsted and Lewis Solid Acid Catalysts in the Valorization of Citronellal Federica Zaccheria 1, Federica Santoro 1, Elvina Dhiaul Iftitah 2 and Nicoletta Ravasio 1,* 1 CNR Institute of Molecular Science and Technology, Via Golgi 19, 20133 Milano, Italy; [email protected] (F.Z.); [email protected] (F.S.) 2 Chemistry Department Faculty of Science, Brawijaya University Jl. Veteran, Malang 65145, Indonesia; [email protected] * Correspondence: [email protected]; Tel.: +39-02-5031-4382 Received: 30 July 2018; Accepted: 12 September 2018; Published: 22 September 2018 Abstract: Terpenes are valuable starting materials for the synthesis of molecules that are of interest to the flavor, fragrance, and pharmaceutical industries. However, most processes involve the use of mineral acids or homogeneous Lewis acid catalysts. Here, we report results obtained in the liquid-phase reaction of citronellal with anilines under heterogeneous catalysis conditions to give tricyclic compounds with interesting pharmacological activity. The terpenic aldehyde could be converted into octahydroacridines with a 92% yield through an intramolecular imino Diels–Alder reaction of the imine initially formed in the presence of an acidic clay such as Montmorillonite KSF. Selectivity to the desired product strongly depended on the acid sites distribution, with Brønsted acids favoring selectivity to octahydroacridine and formation of the cis isomer. Pure Lewis acids such as silica–alumina with a very low amount of alumina gave excellent results with electron-rich anilines like toluidine and p-anisidine. This protocol can be applied starting directly from essential oils such as kaffir lime oil, which has a high citronellal content.
    [Show full text]
  • Asymmetric Catalysis in Aqueous Media*
    Pure Appl. Chem., Vol. 79, No. 2, pp. 235–245, 2007. doi:10.1351/pac200779020235 © 2007 IUPAC Asymmetric catalysis in aqueous media* Shu– Kobayashi Graduate School of Pharmaceutical Sciences, The University of Tokyo, The HFRE Division, ERATO, Japan Science and Technology Agency (JST), Hongo, Bunkyo-ku, Tokyo 113-0033, Japan Abstract: Lewis acid catalysis has attracted much attention in organic synthesis because of unique reactivity and selectivity attained under mild conditions. Although various kinds of Lewis acids have been developed and applied in industry, these Lewis acids must be gener- ally used under strictly anhydrous conditions. The presence of even a small amount of water handles the reactions owing to preferential reactions of the Lewis acids with water rather than the substrates. In contrast, rare earth and other metal complexes have been found to be water- compatible. Several catalytic asymmetric reactions in aqueous media, including hydroxy- methylation of silicon enolates with an aqueous solution of formaldehyde in the presence of Sc(OTf)3–chiral bipyridine ligand or Bi(OTf)3–chiral bipyridine ligand, Sc- or Bi-catalyzed asymmetric meso-epoxide ring-opening reactions with amines, and asymmetric Mannich- type reactions of silicon enolates with N-acylhydrazones in the presence of a chiral Zn cata- lyst have been developed. Water plays key roles in these asymmetric reactions. Keywords: reactions in aqueous media; Lewis acids; catalytic asymmetric reactions; hydroxymethylation of silicon enolates; Sc(OTf)3–chiral bipyridine ligand. INTRODUCTION Organic reactions in aqueous media are of current interest owing to the key role played by water as a solvent for green chemistry [1].
    [Show full text]
  • Ester Hydrolysis: Conditions for Acid Autocatalysis and a Kinetic Switch
    This is a repository copy of Ester hydrolysis: Conditions for acid autocatalysis and a kinetic switch. White Rose Research Online URL for this paper: http://eprints.whiterose.ac.uk/116706/ Version: Accepted Version Article: Bánsági, T. and Taylor, A.F. orcid.org/0000-0003-0071-8306 (2017) Ester hydrolysis: Conditions for acid autocatalysis and a kinetic switch. Tetrahedron, 73 (33). pp. 5018-5022. ISSN 0040-4020 https://doi.org/10.1016/j.tet.2017.05.049 Article available under the terms of the CC-BY-NC-ND licence (https://creativecommons.org/licenses/by-nc-nd/4.0/ Reuse This article is distributed under the terms of the Creative Commons Attribution-NonCommercial-NoDerivs (CC BY-NC-ND) licence. This licence only allows you to download this work and share it with others as long as you credit the authors, but you can’t change the article in any way or use it commercially. More information and the full terms of the licence here: https://creativecommons.org/licenses/ Takedown If you consider content in White Rose Research Online to be in breach of UK law, please notify us by emailing [email protected] including the URL of the record and the reason for the withdrawal request. [email protected] https://eprints.whiterose.ac.uk/ Accepted Manuscript Ester hydrolysis: Conditions for acid autocatalysis and a kinetic switch Tamás Bánsági, Annette F. Taylor PII: S0040-4020(17)30537-9 DOI: 10.1016/j.tet.2017.05.049 Reference: TET 28715 To appear in: Tetrahedron Received Date: 2 April 2017 Revised Date: 10 May 2017 Accepted Date: 12 May 2017 Please cite this article as: Bánsági Tamá, Taylor AF, Ester hydrolysis: Conditions for acid autocatalysis and a kinetic switch, Tetrahedron (2017), doi: 10.1016/j.tet.2017.05.049.
    [Show full text]
  • Paul M a & Long F A. HO and Related Indicator Acidity Functions. Chem. Rev. 57:1-45, 1957
    Number 4 January 23, 1978 Citation Classics Paul M A & Long F A. HO and related indicator acidity functions. Chem. Rev. 57:1-45, 1957. The authors review the literature pertaining to function (a logarithmic measure of acidity indicator acidity functions and their reducing to pH in dilute aqueous solutions) is applications to elucidating the mechanisms of derived from indicators of charge type: B° + H+ acid catalysis. [The SCI® indicates $$$ BH + that this paper was cited 699 times in “In concentrated aqueous solutions of strong the period 1961-1976.] acids, HO is observed to decrease (indicating increasing acidity) with increasing acid concentration C significantly more rapidly than does -log C, and furthermore the HO values for the different strong acids are spread apart. Since the rates of certain acid- Professor M. A. Paul (retired) catalyzed reactions were found to correlate and Professor FA. Long rather well with the behavior of HO whereas Department of Chemistry the rates of others showed poor correlation, Cornell University interest grew in the possibility of using the Ithaca, New York 14853 presence or absence of such correlation as evidence for the particular mechanism of acid catalysis involved. Our review was prepared January 31, 1977 at a time when interest in acid catalysis had been renewed by the ideas of C.K. Ingold and his associates on the mechanisms of homogeneous organic reactions in general. By “This article, together with a companion assembling and critically evaluating the article on the application of the HO acidity published data on acidity functions and their function to kinetics and mechanisms of acid applications to the study of acid catalysis (252 catalysis, 1 reviewed twenty-five years of references), we evidently helped many research stemming from the establishment by investigators in further research on the subject.
    [Show full text]
  • Phosphomolybdic Acid Catalysis of Cellulose Hydrolysis Troy R
    East Tennessee State University Digital Commons @ East Tennessee State University Undergraduate Honors Theses Student Works 5-2017 Phosphomolybdic Acid Catalysis of Cellulose Hydrolysis Troy R. Dolmetsch East Tennessee State University Follow this and additional works at: https://dc.etsu.edu/honors Part of the Analytical Chemistry Commons, Environmental Chemistry Commons, and the Sustainability Commons Recommended Citation Dolmetsch, Troy R., "Phosphomolybdic Acid Catalysis of Cellulose Hydrolysis" (2017). Undergraduate Honors Theses. Paper 413. https://dc.etsu.edu/honors/413 This Honors Thesis - Withheld is brought to you for free and open access by the Student Works at Digital Commons @ East Tennessee State University. It has been accepted for inclusion in Undergraduate Honors Theses by an authorized administrator of Digital Commons @ East Tennessee State University. For more information, please contact [email protected]. Phosphomolybdic Acid Catalysis of Cellulose Hydrolysis Author: Troy Dolmetsch Research Advisor: Dr. Dane W. Scott Department of Chemistry at East Tennessee State University Spring 2017 Abstract Renewable sources such as cellulose derived biofuels are sought after in order to replace fossil fuel sources that are currently used to meet energy demands. Cellulose is a biological polymer composed of a chain of glucose molecules. Hydrolysis of cellulosic materials then has potential to serve as a source of renewable energy in the form of biofuels. The crystalline structure of cellulose is very stable, and current methods of catalyzed hydrolysis are inefficient for industrial application. This project explores the use of phosphomolybdic acid (PMA) in water to catalyze hydrolysis of microcrystalline cellulose. Temperature of hydrolysis was varied from 40 °C – 100 °C. The amount of soluble hydrolysis product was determined through wet oxidative total organic carbon analysis using a Hach method kit.
    [Show full text]