PDE for 2-Methyletrahydrofuran
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Energy-Saving Reduced-Pressure Extractive Distillation with Heat
Energy-Saving Reduced-Pressure Extractive Distillation with Heat Integration for Separating the Biazeotropic Ternary Mixture Tetrahydrofuran–Methanol–Water Jinglian Gu, Xinqiang You, Changyuan Tao, Jun Li, Vincent Gerbaud To cite this version: Jinglian Gu, Xinqiang You, Changyuan Tao, Jun Li, Vincent Gerbaud. Energy-Saving Reduced- Pressure Extractive Distillation with Heat Integration for Separating the Biazeotropic Ternary Mixture Tetrahydrofuran–Methanol–Water. Industrial and engineering chemistry research, American Chemical Society, 2018, 57 (40), pp.13498-13510. 10.1021/acs.iecr.8b03123. hal-01957130 HAL Id: hal-01957130 https://hal.archives-ouvertes.fr/hal-01957130 Submitted on 17 Dec 2018 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. OATAO is an open access repository that collects the work of Toulouse researchers and makes it freely available over the web where possible This is an author’s version published in: http://oatao.univ-toulouse.fr/21066 Official URL: https://doi.org/10.1021/acs.iecr.8b03123 To cite this version: Gu, Jinglian and You, Xinqiang and Tao, Changyuan and Li, Jun and Gerbaud, Vincent Energy-Saving Reduced-Pressure Extractive Distillation with Heat Integration for Separating the Biazeotropic Ternary Mixture Tetrahydrofuran–Methanol–Water. -
Cyclopentyl Methyl Ether (CPME)
Korean J. Chem. Eng., 34(2), 463-469 (2017) pISSN: 0256-1115 DOI: 10.1007/s11814-016-0265-5 eISSN: 1975-7220 INVITED REVIEW PAPER Measurement and correlation of the isothermal VLE data for the binary mixtures of cyclopentene (CPEN)+cyclopentyl methyl ether (CPME) Wan Ju Jeong and Jong Sung Lim† Department of Chemical and Biomolecular Engineering, Sogang University, C.P.O. Box 1142, Seoul 04107, Korea (Received 2 August 2016 • accepted 20 September 2016) Abstract−The isothermal vapor-liquid equilibrium data for the binary systems of cyclopentene (1)+cyclopentyl methyl ether (2) were measured at 313.15, 323.15, 333.15, 343.15 and 353.15 K using a dynamic-type equilibrium apparatus and online gas chromatography analysis. For all the measured VLE data consistency tests were performed for the verifi- cation of data using Barker’s method and the ASPEN PLUS Area Test method. All the resulting average absolute val- δ γ γ ues of residuals [ ln ( 1/ 2)] for Barker’s method and D values for the ASPEN PLUS area test method were com- paratively small. So, the VLE data reported in this study are considered to be acceptable. This binary system shows neg- ative deviation from Raoult’s law and does not exhibit azeotropic behavior at whole temperature ranges studied here. The measured data were correlated with the P-R EoS using the Wong-Sandler mixing rule. The overall average relative deviation of pressure (ARD-P (%)) between experimental and calculated values was 0.078% and that of vapor phase compositions (ARD-y (%)) was 0.452%. Keywords: Vapor Liquid Equilibria (VLE), Cyclopentyl Methyl Ether (CPME), Cyclopentene (CPEN), Peng-Robinson Equation of State (PR-EoS), Wong-Sandler Mixing Rule (WS-MR) INTRODUCTION however, have some disadvantages because they use dimethyl sul- fate and methyl iodide as a reactant, respectively, which are muta- Ethers are widely used in organic chemistry and biochemistry. -
Poly(Ethylene Oxide-Co-Tetrahydrofuran) and Poly(Propylene Oxide-Co-Tetrahydrofuran): Synthesis and Thermal Degradation
Revue Roumaine de Chimie, 2006, 51(7-8), 781–793 Dedicated to the memory of Professor Mircea D. Banciu (1941–2005) POLY(ETHYLENE OXIDE-CO-TETRAHYDROFURAN) AND POLY(PROPYLENE OXIDE-CO-TETRAHYDROFURAN): SYNTHESIS AND THERMAL DEGRADATION Thomas HÖVETBORN, Markus HÖLSCHER, Helmut KEUL∗ and Hartwig HÖCKER Lehrstuhl für Textilchemie und Makromolekulare Chemie der Rheinisch-Westfälischen Technischen Hochschule Aachen, Pauwelsstr. 8, 52056 Aachen, Germany Received January 12, 2006 Copolymers of tetrahydrofuran (THF) and ethylene oxide (EO) (poly(THF-co-EO) and THF and propylene oxide (PO) (poly(THF-co-PO) were obtained by cationic ring opening polymerization of the monomer mixture at 0°C using boron trifluoride etherate (BF3.OEt2) as the initiator. From time conversion plots it was concluded that both monomers are consumed from the very beginning of the reaction and random copolymers are obtained. For poly(THF-co-PO) the molar ratio of repeating units was varied from [THF]/[PO] = 1 to 10; the molar ratio of monomers in the feed corresponds to the molar ratio of repeating units in the copolymer. Thermogravimetric analysis of the copolymers revealed that both poly(THF-co-EO) and poly(THF-co-PO) decompose by ca. 50°C lower than poly(THF) and by ca. 100°C lower than poly(EO); 50% mass loss is obtained at T50 = 375°C for poly(EO), T50 = 330°C for poly(THF) and at T50 = 280°C for both copolymers. The [THF]/[PO] ratio does not influence the decomposition temperature significantly as well. For the copolymers the activation energies of the thermal decomposition (Ea) were determined experimentally from TGA measurements and by density functional calculations on model compounds on the B3LYP/6-31+G* level of theory. -
(12) United States Patent (10) Patent No.: US 7.494,962 B2 Kinet Al
USOO74949.62B2 (12) United States Patent (10) Patent No.: US 7.494,962 B2 Kinet al. (45) Date of Patent: Feb. 24, 2009 (54) SOLVENTS CONTAINING CYCLOAKYL (56) References Cited ALKYLETHERS AND PROCESS FOR PRODUCTION OF THE ETHERS U.S. PATENT DOCUMENTS 3496,223 A * 2/1970 Mitchell et al. ............... 562/22 (75) Inventors: Idan Kin, Ottawa (CA); Genichi Ohta, Tokyo (JP); Kazuo Teraishi, Tokyo (JP); Kiyoshi Watanabe, Tokyo (JP) (Continued) (73) Assignee: Zeon Corporation, Tokyo (JP) FOREIGN PATENT DOCUMENTS (*) Notice: Subject to any disclaimer, the term of this EP 587434 A1 3, 1994 patent is extended or adjusted under 35 U.S.C. 154(b) by 349 days. (Continued) (21) Appl. No.: 10/481,340 OTHER PUBLICATIONS (22) PCT Filed: Jun. 27, 2002 Edited by Kagaku Daijiten Henshu Iinkai, “Kagaku Daijiten 9”. (86). PCT No.: PCT/UP02/06501 Kyoritsu Shuppan Co., Ltd., Aug. 25, 1962, p. 437, "Yozai'. (Continued) S371 (c)(1), (2), (4) Date: Sep. 24, 2004 Primary Examiner Gregory E Webb (74) Attorney, Agent, or Firm—Birch, Stewart, Kolasch & (87) PCT Pub. No.: WO03/002500 Birch, LLP PCT Pub. Date: Jan. 9, 2003 (57) ABSTRACT (65) Prior Publication Data The present inventions are (A) a solvent comprising at least US 2005/OO65060A1 Mar. 24, 2005 one cycloalkyl alkyl ether (1) represented by the general O O formula: R1-O R2 (wherein R1 is cyclopentyl or the like: (30) Foreign Application Priority Data and R2 is C1-10 alkyl or the like); (B) a method of prepara Jun. 28, 2001 (JP) ............................. 2001-196766 tions the ethers (1) characterized by reacting an alicyclic Oct. -
Tetrahydrofuran
SOME CHEMICALS THAT CAUSE TUMOURS OF THE URINARY TRACT IN RODENTS VOLUME 119 This publication represents the views and expert opinions of an IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, which met in Lyon, 6–13 June 2017 LYON, FRANCE - 2019 IARC MONOGRAPHS ON THE EVALUATION OF CARCINOGENIC RISKS TO HUMANS TETRAHYDROFURAN 1. Exposure Data Boiling point: 65–66 °C (EPA, 2012) Melting point: −108.44 °C (ECHA, 2018) 1.1 Identification of the agent Relative density: 0.883 at 25 °C (water, 1) (ECHA, 2018) 1.1.1 Nomenclature Solubility: Miscible in water (ECHA, 2018) Chem. Abstr. Serv. Reg. No.: 109-99-9 Volatility: Vapour pressure, 19.3 kPa at 20 °C (IPCS, 1997) EC/List No.: 203-726-8 Relative vapour density: 2.5 (air = 1); relative Chem. Abstr. Serv. name: Tetrahydrofuran density of the vapour/air mixture at 20 °C IUPAC systematic name: Oxolane (air = 1): 1.28 (IPCS, 1997) Synonyms: Butane alpha,delta-oxide; butane, Stability: Tetrahydrofuran is prone to oxida- 1,4-epoxy-; cyclotetramethylene oxide; dieth- tion to peroxides, butyric acid, butyralde- ylene oxide; 1,4-epoxybutane; furan, tetra- hyde, and related compounds, mainly on hydro-; furanidine; hydrofuran; oxacyclo- ageing and in the presence of light, heat, pentane; tetramethylene oxide; THF and moisture. The formation of peroxides can be retarded by adding stabilizers such as 1.1.2 Structural and molecular formulae, and hydroquinone or 2,6-di-tert-butyl-p-cresol at relative molecular mass 250 mg/kg (Coetzee & Chang, 1985; Müller, 2012). O Flash point: −14.5 °C -
United States Patent 0 Ice Patented Jan
3,489,528 United States Patent 0 ice Patented Jan. 13, 1970 1 2 number of (BHZNHZ) groups, but the product is con 3,489,528 PREPARATION OF POLYAMINOBORANES sistent in composition, as shown by infra-red and ele William E. Zanieski, Pittsburgh, Pa., assignor to Mine mental analyses, and the average value of n is about 4. Safety Appliances Company, a corporation of In another example a solution of THF-EH3 contain— Pennsylvania ing 2.99 g. of B2H6 in 150 ml. of THF was prepared N0 Drawing. Filed Apr. 5, 1965, Ser. No. 445,707 in the same manner as the previous example and the Int. Cl. C01b 21/00 solution was warmed to -30° C. 3.12 g. of gaseous US. Cl. 23—358 6 Claims ammonia was bubbled into and dissolved in the solution at —30° C. and the resultant clear solution was warmed to 0° C, at which temperature hydrogen was evolved and polyaminoborane, identical to that obtained in the ABSTRACT OF THE DISCLOSURE previous example, precipitated from the reaction mix Ammonia and diborane are reacted in tetrahydrofuran ture. at a temperature below about —30° C.; polyaminoboranes ‘Although the invention is not limited to any particular are precipitated when the reaction mixture is warmed. 15 reaction mechanism, it appears that the reaction of NH3 Aging of an ammonia solution of the polyaminoboranes and BZHS in THF forms an intermediate that is formed so produced yields an ammonia insoluble, more highly and is stable only at temperatures below about —30° C. polymerized polyaminoborane. and that this intermediate decomposes at temperatures above about —30° C. -
Tetrahydrofuran (THF)
Tetrahydrofuran (THF) Typical Physical Properties of THF Molecular Weight 72.11 g/mol Empirical Formula C4H8O Appearance Colorless Freezing Point ‐108°C (‐ 164.4°F) Flash Point – Closed Cup ‐20°C (‐4°F) Boiling Point @ 760mmHg 66°C (150.8°F) Autoignition Temperature 230°C (446°F) Density @ 20°C 0.89 kg/l Tetrahydrofuran (THF) is a clear, colorless liquid with 7.43 lb/gal an ether‐like odor. The principal end uses of THF Vapor Pressure @ 20°C 193 hPa include PTMEG, pharmaceutical solvent, adhesives, PVC cement and magnetic tape. Due to its' tendency Evaporation Rate (nBuAc = 1) 8 to form peroxides during storage, THF is inhibited with Solubility @ 20°C (in Water) Complete BHT. Refractive Index @ 20°C 1.407 CAS number Viscosity @ 20°C 0.516 cP Lower Flammability in Air 1.5% v/v 109‐99‐9 Upper Flammability in Air 12.4% v/v Synonyms Note: The properties reported above are typical physical properties. Monument Chemical in no way guarantees that the 1,4‐epoxybutane; Cyclotetramethylene oxide; Butane product from any particular lot will conform exactly to the given .alpha.,.delta.‐oxide values. Health and safety information Under current U.S. OSHA's Hazardous Communication program THF is classified as a flammable liquid, can cause eye and respiratory irritation. Keep the material away from heat sources, hot surfaces, open flames, and sparks. Use only in a well‐ventilated area. Observe good industrial hygiene practices and use appropriate Personal Protective Equipment. For full safety information please refer to the Safety Data Sheet. Storage and Handling specific product Technical Data Sheet (TDS) is accurate, but makes no representations as to the sufficiency or THF should be stored only in tightly closed, properly completeness of the product or information in this TDS vented containers away from heat, sparks, open flame and makes no commitment to correct or bring up‐to‐date or strong oxidizing agents. -
Isobutanol in Marine Gasoline
Isobutanol in Marine Gasoline Glenn Johnston July 11, 2017 Bioeconomy 2017 Washington D.C. 1B: Drivers for Emergence of Biofuels for Maritime Industry © 2012 Gevo, Inc. | 1 Gevo’s Current Business System Gevo Production Facilities Core Near Term Markets Isobutanol Production – Side-by-Side with Ethanol Drop-in Markets - Isobutanol Luverne, MN Isobutanol Specialty Chemicals & Solvents Specialty Gasoline Blendstock (Marine/Off-Road) 15 MGPY EtOH 1.5 MGPY IBA* Isobutanol Hydrocarbon Biorefinery Drop-in Markets - Hydrocarbons South Hydrocarbons Hampton Jet Fuel Resources Silsbee, TX Isooctane (gasoline) © 2016 Gevo, Inc. | 2 Isobutanol Properties Gasoline blending value Gasoline Ethanol Isobutanol RON 95 109 105 MON 85 90 91 Anti-knock Index 90 100 98 RVP (psi) 7-15 19 5.2 Density 20C [kg/m3] 720-775 794 801 Boiling Point (C) 32.2 21.1 26.6 % Heating Value of Gasoline 100 66 84 Oxygen (%w/w) <2.7% 34.7 21.6 isobutanol has low RVP, enabling refiners to blend incremental volumes of butanes and pentanes Marine Research Overview Marine Engine Tested – BRP Envinrude and SeaDoo, Mercury, Volvo-Penta, Yamaha, Tohatsu, Indmar, OMC-Johnson, Honda. Marine Biobutanol over 5 years of research -Alternative Fuel Butanol: Preliminary Investigation on Performance and Emissions of a Marine Two-Stroke Direct Fuel Injection Engine -Impact of Blending Gasoline with lsobutanol Compared to Ethanol on Efficiency, Performance and Emissions of a Recreational Marine 4-Stroke Engine -Gaseous and Particulate Emissions Using Isobutanol-Extended Fuel in Recreational Marine -
Contribution of Cyclopentyl Methyl Ether (CPME) to Green Chemistry
sustainability / green chemistry Industry perspective Shunji Sakamoto Contribution of Cyclopentyl Methyl Ether (CPME) to Green Chemistry Shunji sakamoto Specialty Chemicals Division, ZEON CORPORATION, 1-6-2 Marunouchi, Chiyoda-ku, Tokyo, 1008246, Japan easy peroxide formation and water miscibility, the demand KEyWORDS for CPME has steadily been growing in the pharmaceutical Cyclopentyl methyl ether, CPME, Green Chemistry, industry as well as in the electronic and fragrance solvent, process, ICH. industries. Also, CPME has been registered or listed in the corresponding legislations for new chemical substances of United States of America, Canada, European Union, ABSTRACT Japan, South Korea, China and Chinese Taipei, and is commercially available in these countries and regions as Cyclopentyl methyl ether (CPME) is an alternative well as others including India. solvent and has preferable properties including higher In this article, I answer the question why CPME is “Green” hydrophobicity, lower formation of peroxides and better even though it is derived from petroleum. stability under acidic and basic conditions compared to other traditional ether solvents such as tetrahydrofuran. Due to the above unique properties, CPME has particular UNIQUE FEATURES OF CPME 24 advantages and renders some conventional reaction sequences in one pot or easier process as a result of CPME is an asymmetric aliphatic ether having a cyclopentyl solvent unification and facile isolation of the products, group. It has seven unique features attributed to its structure which contribute to Green Chemistry as well as to (Table 1). process innovation. CPME meets eight definitions out of the 12 Principles of Green Chemistry (1) because of Extremely lower miscibility with water the above characteristics as well as its manufacturing The solubility of CPME in water is only 1.1% and that of water process and its applications. -
Next Generation Biofuels
Photo-Synthetic Biology for Fuels James C. Liao Chemical and Biomolecular Engineering University of California, Los Angeles The Current Biofuel Cycle CO2 CO2 Ethanol Biodiesel The Direct Solar Fuel Cycle CO2 CO2 Higher Alcohols Biofuels Long chain Ethanol alcohols/alkanes Energy content Low High Hygroscopicity High Low Vehicle Yes No retrofitting? Vapor pressure High Low Production High Zero/Low yield Higher alcohols Native producers? yes Iso-propanol no n-propanol yes n-butanol no Iso-butanol no 2-methyl-1-butanol no 3-methyl-1-butanol Pathways for alcohol synthesis CoA-dependent pathway Pyruvate PDH NADH Acetyl-CoA Acetaldehyde NADH NADH ADH Acetoacetyl-CoA Ethanol 3-Hydroxybutyryl-CoA Crotonyl-CoA Butyryl-CoA Butyraldehyde n-Butanol Alternative Pathways to Make Alcohols CoA-dependent pathway Pyruvate Non-CoA pathway PDH NADH PDC Acetyl-CoA Acetaldehyde NADH NADH ADH ? Acetoacetyl-CoA Ethanol 3-Hydroxybutyryl-CoA Crotonyl-CoA Butyryl-CoA Butyraldehyde n-Butanol Atsumi et al. Nature 2008 Generalization of keto acid decarboxylase chemistry Longer chain keto acids A simple keto acid Pyruvate 2-keto acid PDC KDC Acetylaldehyde R-aldehyde ADH ADH Ethanol R-OH Ehrlich, F. Ber. Dtsch. Chem. Ges.1907 Opening the active site Zymomonas mobilis PDC Lactococcus lactis KdcA E.coli Long Chain 2-keto acids KDC 2-keto acids) R-aldehyde ADH 2008 2-phenylethanol (from Nature 3-M-1-butanol et al. 2-M-1-butanol p henylpyruvate Atsumi Production of Higher Alcohols1-butanol in 2-keto-4-methyl-pentanoate 2-keto-3-methyl-valerate isobutanol 2-ketovalerate 1-propanol 2-ketoisovalerate Production (mM) Production 2-ketobutyrate ํC 40hr 30 Further generalization of alcohol‐ producing chemistry Atsumi et al. -
Q3C (R8): Impurities: Guideline for Residual Solvents Step 2B
04 May 2020 EMA/CHMP/ICH/213867/2020 Committee for Medicinal Products for Human Use Q3C (R8): Impurities: guideline for residual solvents Step 2b Transmission to CHMP 30 April 2020 Adoption by CHMP 30 April 2020 Release for public consultation 4 May 2020 Deadline for comments 30 July 2020 Comments should be provided using this template. The completed comments form should be sent to [email protected] 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 6000An agency of the European Union © European Medicines Agency, 2020. Reproduction is authorised provided the source is acknowledged. PDE for 2-Methyltetrahydrofuran, Cyclopentyl Methyl Ether, and Tertiary-Butyl Alcohol INTERNATIONAL COUNCIL FOR HARMONISATION OF TECHNICAL REQUIREMENTS FOR PHARMACEUTICALS FOR HUMAN USE ICH HARMONISED GUIDELINE IMPURITIES: GUIDELINE FOR RESIDUAL SOLVENTS Q3C(R8) PDE FOR 2-METHYLTETRAHYDROFURAN, CYCLOPENTYL METHYL ETHER, AND TERTIARY-BUTYL ALCOHOL Draft version Endorsed on 25 March 2020 Currently under public consultation Note : This document contains only the PDE levels for three solvents: 2- methyltetrahydrofuran, cyclopentylmethylether and tert-butanol that were agreed to be included in the ICH Q3C(R8) revision. Further to reaching Step 4, these PDEs would be integrated into a complete Q3C(R8) Guideline document. At Step 2 of the ICH Process, a consensus draft text or guideline, agreed by the appropriate ICH Expert Working Group, is transmitted by the ICH Assembly to the regulatory authorities PDE for 2-Methyltetrahydrofuran, Cyclopentyl Methyl Ether, and Tertiary-Butyl Alcohol of the ICH regions for internal and external consultation, according to national or regional procedures. -
Method MD-99 Polar Volatile Organic Compounds in Pulp Industry Wastewaters by Microdistillation and GC-FID
NCASI METHOD MD-99 POLAR VOLATILE ORGANIC COMPOUNDS IN PULP INDUSTRY WASTEWATERS BY MICRODISTILLATION AND GC-FID NCASI West Coast Regional Center Organic Analytical Program July 1999 Acknowledgments This method is authored by Alex Gholson, Senior Research Scientist, and Dean Hoy, Research Associate, with assistance from Diana Cook, Senior Research Scientist, all of NCASI West Coast Regional Center. Mark Bruce of Wadsworth Alert Labs (now Quanterra) developed the microdistillation technique and also provided valuable input during development of this method. For more information about this method, contact: Alex Gholson, Ph.D. John Pinkerton, Ph.D. Senior Research Scientist Vice President, Air Quality NCASI West Coast Regional Center NCASI P.O. Box 458 P.O. Box 13318 Corvallis, OR 97339 Research Triangle Park, NC 27709 (541) 752-8801 (919) 558-1992 [email protected] [email protected] For information about NCASI publications, contact: Publications Coordinator NCASI PO Box 13318 Research Triangle Park, NC 27709 (919) 558-1999 [email protected] National Council for Air and Stream Improvement, Inc. (NCASI). 2000. Methods Manual - Polar volatile organic compounds in pulp industry wastewaters by microdistillation and GC-FID. Research Triangle Park, NC: National Council for Air and Stream Improvement, Inc. 2000 by the National Council for Air and Stream Improvement, Inc. Disclaimer: The mention of trade names or commercial products does not constitute endorsement or recommendation for use. The microdistillation step has been included in the Third Update of SW-846 as Method 5031. This method is included in the NCASI Methods Manual as a PROPOSED method. The purpose of including proposed methods in the NCASI Methods Manual is to make it known that a method is under development and to solicit comment regarding the technical merit and applicability of the method.