Solvent Compatibility of Poly(Dimethylsiloxane)-Based Microfluidic Devices
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
Kinetic Modeling and Mechanistic Investigations of Transesterification of Propylene Carbonate with Methanol Over Fe-Mn Double Metal Cyanide Catalyst
Reaction Chemistry & Engineering Kinetic Modeling and Mechanistic Investigations of Transesterification of Propylene Carbonate with Methanol over Fe-Mn Double Metal Cyanide Catalyst Journal: Reaction Chemistry & Engineering Manuscript ID RE-ART-09-2019-000372.R1 Article Type: Paper Date Submitted by the 21-Oct-2019 Author: Complete List of Authors: Song, Ziwei; Yanshan University, Subramaniam, Bala; University of Kansas, Center for Environmentally Beneficial Catalysis Chaudhari, Raghunath; University of Kansas, Chemical & Petroleum Engineering Page 1 of 23 Reaction Chemistry & Engineering Kinetic Modeling and Mechanistic Investigations of Transesterification of Propylene Carbonate with Methanol over Fe-Mn Double Metal Cyanide Catalyst Ziwei Song, a,b,c Bala Subramaniam, a,b and Raghunath V. Chaudhari* a,b aCenter for Environmentally Beneficial Catalysis, University of Kansas, 1501 Wakarusa Dr. Lawrence, KS 66047, United States bDepartment of Chemical & Petroleum Engineering, University of Kansas, 1503 W 15th St. Lawrence, KS 66045, United States cDepartment of Chemical Engineering, College of Environmental and Chemical Engineering, Yanshan University, Qinhuangdao 066004, China *Corresponding author: [email protected] KEYWORDS: double metal cyanide, transesterification, dimethyl carbonate, microkinetic modeling 1 Reaction Chemistry & Engineering Page 2 of 23 Abstract Kinetic modeling of transesterification of propylene carbonate with methanol using Fe-Mn double metal cyanide catalyst has been investigated based on experimental data obtained under kinetically controlled conditions in a batch slurry reactor in the 140-200 °C range. A simple two-step power law model was found to represent the experimental data well. In addition, a detailed kinetic model based on a molecular level description of the reaction mechanism is also evaluated to provide better insight into the reaction mechanism. -
Study of Various Aqueous and Non-Aqueous Amine Blends for Hydrogen Sulfide Removal from Natural Gas
processes Article Study of Various Aqueous and Non-Aqueous Amine Blends for Hydrogen Sulfide Removal from Natural Gas Usman Shoukat , Diego D. D. Pinto and Hanna K. Knuutila * Department of Chemical Engineering, Norwegian University of Science and Technology (NTNU), 7491 Trondheim, Norway; [email protected] (U.S.); [email protected] (D.D.D.P.) * Correspondence: [email protected] Received: 8 February 2019; Accepted: 8 March 2019; Published: 15 March 2019 Abstract: Various novel amine solutions both in aqueous and non-aqueous [monoethylene glycol (MEG)/triethylene glycol(TEG)] forms have been studied for hydrogen sulfide (H2S) absorption. The study was conducted in a custom build experimental setup at temperatures relevant to subsea operation conditions and atmospheric pressure. Liquid phase absorbed H2S, and amine concentrations were measured analytically to calculate H2S loading (mole of H2S/mole of amine). Maximum achieved H2S loadings as the function of pKa, gas partial pressure, temperature and amine concentration are presented. Effects of solvent type on absorbed H2S have also been discussed. Several new solvents showed higher H2S loading as compared to aqueous N-Methyldiethanolamine (MDEA) solution which is the current industrial benchmark compound for selective H2S removal in natural gas sweetening process. Keywords: H2S absorption; amine solutions; glycols; desulfurization; aqueous and non-aqueous solutions 1. Introduction Natural gas is considered one of the cleanest forms of fossil fuel. Its usage in industrial processes and human activities is increasing worldwide, providing 23.4% of total world energy requirement in 2017 [1]. Natural gas is half of the price of crude oil and produces 29% less carbon dioxide than oil per unit of energy output [2]. -
Propylene Carbonate Extraction for Recovery of Poly-3-Hydroxybutryate
1 Propylene Carbonate Extraction for Recovery of Poly-3-hydroxybutryate Abstract Propylene Carbonate Distillation Poly -3-hydroxybutryate (PHB) is a biopolymer produced Propylene Carbonate is an organic solvent produced as a storage molecule for energy and carbon under • Waste solution recovered after PHB by combining propylene oxide with carbon dioxide. It is poor growth conditions in certain organisms. PHB is a precipitation consisted of Propylene considered a polar aprotic solvent (no proton to donate) class of polyhydroxyalkanoates (PHAs), which have Carbonate and Ethanol Due to its characteristics (low vapor pressure, stability, similar properties to plastics derived from petroleum. PHB provides an environmentally friendly alternative to and high polarity) it is used in many applications. These include • Through distillation, both the Ethanol production of fibers and textiles, dyeing, personal care agents petroleum -based plastics due to its biodegradability and and Propylene Carbonate have been and cosmetics, and a component of some adhesives. It is also method of production. It can be produced by recovered. considered non-toxic making it more suitable to use at larger recombinant Escherichia coli, harvested from the cell, scales. and recovered. One of the major expenses of • Recovered 70% Propylene producing PHB is the extraction of the PHB from the Carbonate and nearly all Ethanol biomass. This study focused on evaluating different methods of PHB extraction for their ability to effectively • Preliminary experiments show no extract PHB from E. coli biomass and the feasibility of Propylene Carbonate Extraction Procedure Distillation apparatus to recover Propylene difference in the yield of PHB scaling up those processes. These processes provide a Carbonate and Ethanol from waste stream extracted with distilled Propylene 125 L Bioreactor way to produce PHB from growing E. -
US5349077.Pdf
|||||||||||||||| USOO5349077A United States Patent (19) 11 Patent Number: 5,349,077 Doya et al. 45 Date of Patent: Sep. 20, 1994 54 PROCESS FOR PRODUCING ALKYLENE 5,003,084 3/1991 Su et al. .............................. 549/230 CARBONATES FOREIGN PATENT DOCUMENTS 75 Inventors: Masaharu Doya; Takashi Ohkawa; Yutaka Kanbara; Aksushi Okamoto; 0443758 8/1991 European Pat. Off. Kenichi Kimizuka, all of Niigata, OTHER PUBLICATIONS Japan Chemical Abstracts, vol. 82, No. 23, Jun. 9, 1975, Co 73 Assignee: Mitsubishi Gas Chemical Company, lumbus, Ohio; Sergio Fumasoni et al. Inc., Tokyo, Japan Primary Examiner-José G. Dees 21 Appl. No.: 99,461 Assistant Examiner-Joseph M. Conrad, III 22 Filed: Jul. 30, 1993 Attorney, Agent, or Firm-Wenderoth, Lind & Ponack (30) Foreign Application Priority Data (57) ABSTRACT Jul. 31, 1992 JP Japan .................................. 4-205362 A process for producing alkylene carbonates which Jul. 31, 1992 (JP) Japan .......................... ... 4-205363 comprises reacting urea and glycols described by the Jul. 31, 1992 JP Japan .......................... ... 4-205364 general formula RCH(OH) CH2OH; wherein R repre Jun. 30, 1993 JP Japan .................................. 5-161857 sents hydrogen or an alkyl group containing 1 to 4 51) Int. Cl. .............................................. CO7C 69/96 carbons, using a catalyst containing zinc, magnesium, 52 U.S. Cl. .................................... 558/260; 549/229; lead or calcium at reduced pressures. The alkylene 549/230 carbonates are produced with high yield easily using 58 Field of Search ................. 558/260; 549/229, 230 raw materials which are comparatively inexpensive with a mild reaction that does not involve explosive or 56) References Cited hazardous materials. U.S. PATENT DOCUMENTS 2,773,881 12/1956 Dunn et al. -
Nitrosamines EMEA-H-A5(3)-1490
25 June 2020 EMA/369136/2020 Committee for Medicinal Products for Human Use (CHMP) Assessment report Procedure under Article 5(3) of Regulation EC (No) 726/2004 Nitrosamine impurities in human medicinal products Procedure number: EMEA/H/A-5(3)/1490 Note: Assessment report as adopted by the CHMP with all information of a commercially confidential nature deleted. Official address Domenico Scarlattilaan 6 ● 1083 HS Amsterdam ● The Netherlands Address for visits and deliveries Refer to www.ema.europa.eu/how-to-find-us Send us a question Go to www.ema.europa.eu/contact Telephone +31 (0)88 781 6000 An agency of the European Union © European Medicines Agency, 2020. Reproduction is authorised provided the source is acknowledged. Table of contents Table of contents ...................................................................................... 2 1. Information on the procedure ............................................................... 7 2. Scientific discussion .............................................................................. 7 2.1. Introduction......................................................................................................... 7 2.2. Quality and safety aspects ..................................................................................... 7 2.2.1. Root causes for presence of N-nitrosamines in medicinal products and measures to mitigate them............................................................................................................. 8 2.2.2. Presence and formation of N-nitrosamines -
Stable Lithium Diisopropylamide and Method of Preparation
Europaisches Patentamt J European Patent Office Publication number: 0 205 583 Office europeen des brevets B1 EUROPEAN PATENT SPECIFICATION (45) Date of publication of patent specification: 30.01.91 Intel.5: C 07 C 211/65 (3) Application number: 86900522.3 @ Date of filing: 17.12.85 (8) International application number: PCT/US85/02509 ® International publication number: WO 86/03744 03.07.86 Gazette 86/14 STABLE LITHIUM DIISOPROPYLAMIDE AND METHOD OF PREPARATION. (M) Priority: 24.12.84 US 685318 Proprietor: LITHIUM CORPORATION OF AMERICA, INC. Post Office Box 795 Date of publication of application: Bessemer City, NC 28016 (US) 30.12.86 Bulletin 86/52 Inventor: MORRISON, Robert, Charles Publication of the grant of the patent: 1946 Elmwood Drive 30.01.91 Bulletin 91/05 Gastonia, NC 28054 (US) Inventor: HALL, Randy, Winf red Route 4 Box 697 (M) Designated Contracting States: Kings Mountain, NC 28086 (US) AT BE CH DE FR GB IT LI LU NL SE Inventor: RATHMAN, Terry, Lee 3843 Gardner Park Drive Gastonia, NC 28054 (US) References cited: US-A-3197 516 US-A-3 694516 US-A-3388178 US-A-4 006187 Representative: Gore, Peter Manson et al US-A-3446 860 US-A-4399 078 W.P. THOMPSON & CO. Coopers Building Church Street JOURNAL OF ORGANOMETALLIC CHEMISTRY, Liverpool L1 3AB (GB) vol. 4, 1965; GILMAN et al.: "Stabilities of some n-alkyllithium compounds in mixed solvent CO I References cited: 00 systems", pp. 483-487 JOURNAL OF ORGANOMETTALIC CHEMISTRY, m JOURNAL OF AMERICAN CHEMICAL SOCIETY, vol. 29, 1971; HONEYCUTT: "Kinetics of the in vol. -
Green Chemistry
Green Chemistry View Article Online PAPER View Journal | View Issue The greening of peptide synthesis† Cite this: Green Chem., 2017, 19, Stefan B. Lawrenson, Roy Arav and Michael North* 1685 The synthesis of peptides by amide bond formation between suitably protected amino acids is a funda- mental part of the drug discovery process. However, the required coupling and deprotection reactions are routinely carried out in dichloromethane and DMF, both of which have serious toxicity concerns and generate waste solvent which constitutes the vast majority of the waste generated during peptide syn- thesis. In this work, propylene carbonate has been shown to be a green polar aprotic solvent which can be used to replace dichloromethane and DMF in both solution- and solid-phase peptide synthesis. Solution-phase chemistry was carried out with Boc/benzyl protecting groups to the tetrapeptide stage, no epimerisation occurred during these syntheses and chemical yields for both coupling and de- Received 20th January 2017, protection reactions in propylene carbonate were at least comparable to those obtained in conventional Accepted 1st March 2017 solvents. Solid-phase peptide synthesis was carried out using Fmoc protected amino acids on a DOI: 10.1039/c7gc00247e ChemMatrix resin and was used to prepare the biologically relevant nonapeptide bradykinin with compar- Creative Commons Attribution 3.0 Unported Licence. rsc.li/greenchem able purity to a sample prepared in DMF. Introduction methane mixtures.8 These issues are amplified in solid-phase peptide synthesis7,9 where large excesses of reagents are used Peptides are central compounds in the pharmaceutical indus- and resins are washed multiple times with toxic solvents. -
Catalyst and Method for Production of Alkylamines
Europaisches Patentamt its; European Patent Office © Publication number: 0 127 874 Office europeen des brevets A2 (121 EUROPEAN PATENT APPLICATION © Application number: 84106136.9 © Int. CI.3: C 07 C 85/06 C 07 C 85/08, B 01 J 23/80 @ Date of filing: 29.05.84 © Priority: 01.06.83 US 500037 @ Applicant: LEHIGH UNIVERSITY 28.11.83 US 555579 203 East Parker Avenue Bethlehem, PA 18015(US) © Date of publication of application: @ Inventor: Klier, Kamil 12.12.84 Bulletin 84/50 3474 Lord Byron Drive Bethlehem PA 18017(US) © Designated Contracting States: BE DE FR GB NL @ Inventor: Herman, Richard G. 409 Fifth Street Whitehall PA 18052(US) @ Inventor: Vedage, Gamini A. 532 Carlton Avenue Bethlehem PA 18015IUS) © Representative: Berg, Wilhelm, Dr. et al, Patentanwalte Dr. Berg Dipl.-lng. Stapf Dipl.-lng. Schwabe Dr. Dr. Sandmair Postfach 86 02 45 Stuntzstrasse 16 D-8000 Munchen 86(DE) © Catalyst and method for production of alkylamines. This invention relates to an improved catalyst and method for the selective production of alkylamines. More particularly, it is concerned with the preparation of stable highly active catalysts for producing alkylamines by a cataly- tic reaction of ammonia or substituted amines and binary synthesis gas (CO + H2). Introduction This invention relates to an improved catalyst and method for the selective production of alkylamines. More particularly, it is concerned with the preparation of stable highly active catalysts for producing alkylamines by a catalytic reaction of ammonia, primary amines, or substituted amines and binary synthesis gas (CO + H2), or alcohols. Background of the Invention The preparation of methylamines of general formula (CH3)n NH3-n and (CH3)n NH2-nR occurs by the reactions depicted in equations (1) and (2). -
United States Patent Office Patented Dec
3,60,601 United States Patent Office Patented Dec. 3, 1964 2 fied by oxygen atoms attached to other silicon atoms to 3,60,601 form siloxane linkages, monovalent hydrocarbon radicals, AMNE SALTS OF PHOSPHORIC ACED AND AANE SALS OF CAR30XYECAC AS hydrocarbon radicals which are polyvalent, i.e. which SLANO, CONDENSATON CATALYSTS have a valence higher than one, each valence of which James Franklia Hyde, Midland, Mich, assigaor ig Bow is attached to another silicon atom to form silcarbane Corning Corporation, Midland, Mich., a corporation linkages and similar monovalent and polyvalent hydro of Michigan carbon radicals containing such functions as ether link No Drawing. Filed July 3, 1959, Ser. No. 826,421 ages, aromatic halogen atoms, aliphatic fluorine atoms, 7. Caimas. (C. 260-46.5) hydroxyl groups and nitrile groups. Any aliphatic fluo 0 line atoms should be separated from any silicon atom This invention relates to the use of amine salts as by at least three carbon atoms. catalysts for the condensation of silicon-bonded hydroxyl More specifically, the silicon valences of the organe groups. silicon compound employed in this invention can be The condensation of silicon-bonded hydroxyl groups Satisfied by, for example, any alkyl radical such as the employing as catalysts alkali metal and quaternary am 5 Inethyl, ethyl, isopropyl, tert-butyl, 2-ethylhexyl, dodecyl, Inonium hydroxides and organosilicon salts thereof is ccitadecyl and myricyl radicals; any alkenyl radical such now well known in the art. However, these catalysts have as the vinyl, allyl and hexadienyl radicals; any cycloalkyl a primary disadvantage of breaking siloxane bonds causing radical such as the cyclopentyl and cyclohexyl radicals; random rearrangement of siloxane units in a polymer. -
Dissociation Constants of Organic Acids and Bases
DISSOCIATION CONSTANTS OF ORGANIC ACIDS AND BASES This table lists the dissociation (ionization) constants of over pKa + pKb = pKwater = 14.00 (at 25°C) 1070 organic acids, bases, and amphoteric compounds. All data apply to dilute aqueous solutions and are presented as values of Compounds are listed by molecular formula in Hill order. pKa, which is defined as the negative of the logarithm of the equi- librium constant K for the reaction a References HA H+ + A- 1. Perrin, D. D., Dissociation Constants of Organic Bases in Aqueous i.e., Solution, Butterworths, London, 1965; Supplement, 1972. 2. Serjeant, E. P., and Dempsey, B., Ionization Constants of Organic Acids + - Ka = [H ][A ]/[HA] in Aqueous Solution, Pergamon, Oxford, 1979. 3. Albert, A., “Ionization Constants of Heterocyclic Substances”, in where [H+], etc. represent the concentrations of the respective Katritzky, A. R., Ed., Physical Methods in Heterocyclic Chemistry, - species in mol/L. It follows that pKa = pH + log[HA] – log[A ], so Academic Press, New York, 1963. 4. Sober, H.A., Ed., CRC Handbook of Biochemistry, CRC Press, Boca that a solution with 50% dissociation has pH equal to the pKa of the acid. Raton, FL, 1968. 5. Perrin, D. D., Dempsey, B., and Serjeant, E. P., pK Prediction for Data for bases are presented as pK values for the conjugate acid, a a Organic Acids and Bases, Chapman and Hall, London, 1981. i.e., for the reaction 6. Albert, A., and Serjeant, E. P., The Determination of Ionization + + Constants, Third Edition, Chapman and Hall, London, 1984. BH H + B 7. Budavari, S., Ed., The Merck Index, Twelth Edition, Merck & Co., Whitehouse Station, NJ, 1996. -
2020 Emergency Response Guidebook
2020 A guidebook intended for use by first responders A guidebook intended for use by first responders during the initial phase of a transportation incident during the initial phase of a transportation incident involving hazardous materials/dangerous goods involving hazardous materials/dangerous goods EMERGENCY RESPONSE GUIDEBOOK THIS DOCUMENT SHOULD NOT BE USED TO DETERMINE COMPLIANCE WITH THE HAZARDOUS MATERIALS/ DANGEROUS GOODS REGULATIONS OR 2020 TO CREATE WORKER SAFETY DOCUMENTS EMERGENCY RESPONSE FOR SPECIFIC CHEMICALS GUIDEBOOK NOT FOR SALE This document is intended for distribution free of charge to Public Safety Organizations by the US Department of Transportation and Transport Canada. This copy may not be resold by commercial distributors. https://www.phmsa.dot.gov/hazmat https://www.tc.gc.ca/TDG http://www.sct.gob.mx SHIPPING PAPERS (DOCUMENTS) 24-HOUR EMERGENCY RESPONSE TELEPHONE NUMBERS For the purpose of this guidebook, shipping documents and shipping papers are synonymous. CANADA Shipping papers provide vital information regarding the hazardous materials/dangerous goods to 1. CANUTEC initiate protective actions. A consolidated version of the information found on shipping papers may 1-888-CANUTEC (226-8832) or 613-996-6666 * be found as follows: *666 (STAR 666) cellular (in Canada only) • Road – kept in the cab of a motor vehicle • Rail – kept in possession of a crew member UNITED STATES • Aviation – kept in possession of the pilot or aircraft employees • Marine – kept in a holder on the bridge of a vessel 1. CHEMTREC 1-800-424-9300 Information provided: (in the U.S., Canada and the U.S. Virgin Islands) • 4-digit identification number, UN or NA (go to yellow pages) For calls originating elsewhere: 703-527-3887 * • Proper shipping name (go to blue pages) • Hazard class or division number of material 2. -
These Two Workbooks Are Provided by As a Convenient Introduc
These two workbooks are provided by www.hansen-solubility.com as a convenient introduc They are Copyright © 2013 Prof Steven Abbott If you find bugs/issues or would like extra functionality, please email Steven Abbott [email protected] ction to some of the basic HSP methods HSP Sphere dD dP dH R Good 11 18.4 9.7 8.0 7.1 Bad 11 Test Value 16 7 8 Total 22 Delta 2.4 11.4 10.4 Distance 5.5 RED 0.77 Solvents dD dP dH MVol Score Distance Acetone 15.5 10.4 7 73.8 1 5.915773 Acetonitrile 15.3 18 6.1 52.9 0 10.52754 n-Amyl Acetate 15.8 3.3 6.1 148 0 n-Amyl Alcohol 15.9 5.9 13.9 108.6 0 Benzene 18.4 0 2 52.9 0 11.38507 Benzyl Alcohol 18.4 6.3 13.7 103.8 0 Benzyl Benzoate 20 5.1 5.2 190.3 0 1-Butanol 16 5.7 15.8 92 0 2-Butanol 15.8 5.7 14.5 92 0 n-Butyl Acetate 15.8 3.7 6.3 132.6 0 t-Butyl Acetate 15 3.7 6 134.8 0 t-Butyl Alcohol 15.2 5.1 14.7 96 0 Butyl Benzoate 18.3 5.6 5.5 178.1 0 Butyl Diglycol Acetate 16 4.1 8.2 208.2 0 Butyl Glycol Acetate 15.3 7.5 6.8 171.2 0 n-Butyl Propionate 15.7 5.5 5.9 149.3 0 Caprolactone (Epsilon) 19.7 15 7.4 110.8 0 Chloroform 17.8 3.1 5.7 80.5 1 7.075453 m-Cresol 18.5 6.5 13.7 105 1 6.563973 Cyclohexane 16.8 0 0.2 108.9 0 12.82752 Cyclohexanol 17.4 4.1 13.5 105.7 0 Cyclohexanone 17.8 8.4 5.1 104.2 0 Di-isoButyl Ketone 16 3.7 4.1 177.4 0 Diacetone Alcohol 15.8 8.2 10.8 124.3 0 Diethyl Ether 14.5 2.9 4.6 104.7 0 10.87429 Diethylene Glycol Monobut 16 7 10.6 170.4 0 Dimethyl Cyclohexane 16.1 0 1.1 140 0 Dimethyl Sulfoxide (DMSO) 18.4 16.4 10.2 71.3 1 7.066692 1,4-Dioxane 17.5 1.8 9 85.7 0 8.160898 1,3-Dioxolane