Block Copolymers of Styrene and Ethylene Oxide
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
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. -
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. -
Reinforcement of Styrene Butadiene Rubber Employing Poly(Isobornyl Methacrylate) (PIBOMA) As High Tg Thermoplastic Polymer
polymers Article Reinforcement of Styrene Butadiene Rubber Employing Poly(isobornyl methacrylate) (PIBOMA) as High Tg Thermoplastic Polymer Abdullah Gunaydin 1,2, Clément Mugemana 1 , Patrick Grysan 1, Carlos Eloy Federico 1 , Reiner Dieden 1 , Daniel F. Schmidt 1, Stephan Westermann 1, Marc Weydert 3 and Alexander S. Shaplov 1,* 1 Luxembourg Institute of Science and Technology (LIST), 5 Avenue des Hauts-Fourneaux, L-4362 Esch-sur-Alzette, Luxembourg; [email protected] (A.G.); [email protected] (C.M.); [email protected] (P.G.); [email protected] (C.E.F.); [email protected] (R.D.); [email protected] (D.F.S.); [email protected] (S.W.) 2 Department of Physics and Materials Science, University of Luxembourg, 2 Avenue de l’Université, L-4365 Esch-sur-Alzette, Luxembourg 3 Goodyear Innovation Center Luxembourg, L-7750 Colmar-Berg, Luxembourg; [email protected] * Correspondence: [email protected]; Tel.: +352-2758884579 Abstract: A set of poly(isobornyl methacrylate)s (PIBOMA) having molar mass in the range of 26,000–283,000 g mol−1 was prepared either via RAFT process or using free radical polymerization. ◦ These linear polymers demonstrated high glass transition temperatures (Tg up to 201 C) and thermal Citation: Gunaydin, A.; stability (T up to 230 ◦C). They were further applied as reinforcing agents in the preparation of the Mugemana, C.; Grysan, P.; onset Eloy Federico, C.; Dieden, R.; vulcanized rubber compositions based on poly(styrene butadiene rubber) (SBR). The influence of the Schmidt, D.F.; Westermann, S.; PIBOMA content and molar mass on the cure characteristics, rheological and mechanical properties of Weydert, M.; Shaplov, A.S. -
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. -
Synergistic Effect of 2-Acrylamido-2-Methyl-1-Propanesulfonic Acid on the Enhanced Conductivity for Fuel Cell at Low Temperature
membranes Article Synergistic Effect of 2-Acrylamido-2-methyl- 1-propanesulfonic Acid on the Enhanced Conductivity for Fuel Cell at Low Temperature Murli Manohar * and Dukjoon Kim * School of Chemical Engineering, Sungkyunkwan University, Suwon, Kyunggi 16419, Korea * Correspondence: [email protected] (M.M.); [email protected] (D.K.) Received: 3 November 2020; Accepted: 10 December 2020; Published: 15 December 2020 Abstract: This present work focused on the aromatic polymer (poly (1,4-phenylene ether-ether-sulfone); SPEES) interconnected/ cross-linked with the aliphatic monomer (2-acrylamido -2-methyl-1-propanesulfonic; AMPS) with the sulfonic group to enhance the conductivity and make it flexible with aliphatic chain of AMPS. Surprisingly, it produced higher conductivity than that of other reported work after the chemical stability was measured. It allows optimizing the synthesis of polymer electrolyte membranes with tailor-made combinations of conductivity and stability. Membrane structure is characterized by 1H NMR and FT-IR. Weight loss of the membrane in Fenton’s reagent is not too high during the oxidative stability test. The thermal stability of the membrane is characterized by TGA and its morphology by SEM and SAXS. The prepared membranes improved 1 proton conductivity up to 0.125 Scm− which is much higher than that of Nafion N115 which is 1 0.059 Scm− . Therefore, the SPEES-AM membranes are adequate for fuel cell at 50 ◦C with reduced relative humidity (RH). Keywords: 2-acrylamido-2-methyl-1-propanesulfonic; proton-exchange membrane; conductivity; cross-linking; temperature 1. Introduction Recently, lots of polymer electrolyte membranes have been prepared from the sulfonation of aromatic polymers such as poly(arylene ether sulfone) [1–4] and modified poly(arylene ether sulfone) [5–7] for the application of electrodialysis and fuel cells as their rigid-rod backbone structures are basically quite stable in thermal and mechanical aspects. -
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. -
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. -
1- MANUFACTURING of MATERIAL BASED HYDROGEN FUEL for LIGHTWEIGHT VEHICLES by ALI KHAGHANI a Thesis
MANUFACTURING OF MATERIAL BASED HYDROGEN FUEL FOR LIGHTWEIGHT VEHICLES Item Type text; Electronic Thesis Authors KHAGHANI, ALI Publisher The University of Arizona. Rights Copyright © is held by the author. Digital access to this material is made possible by the University Libraries, University of Arizona. Further transmission, reproduction or presentation (such as public display or performance) of protected items is prohibited except with permission of the author. Download date 23/09/2021 12:36:34 Link to Item http://hdl.handle.net/10150/613155 MANUFACTURING OF MATERIAL BASED HYDROGEN FUEL FOR LIGHTWEIGHT VEHICLES By ALI KHAGHANI ____________________ A Thesis Submitted to The Honors College In Partial Fulfillment of the Bachelors degree With Honors in Chemical Engineering THE UNIVERSITY OF ARIZONA M A Y 2016 Approved by: ____________________________ Dr. Kimberly Ogden Chemical and Environmental Engineering -1- Abstract Vehicles powered by hydrogen fuel cells store hydrogen as a cooled liquid at 20 degrees kelvin or a compressed gas at 10,000 pounds per square inch. An alternative that eliminates the need for these extremes of temperature and pressure is to heat a compound containing covalently bonded hydrogen, causing it to release the hydrogen to the fuel cell. Ammonia borane, which is stable at ambient conditions, requires minimal energy for dehydrogenation, and is rich in hydrogen, is a possible storage medium for hydrogen. If a viable storage system could be engineered, demand for ammonia borane as a source of hydrogen would increase. The goal of this project is to develop a processing plant and to optimize design specifications for scaling up processing of ammonia borane through the metathesis reaction pathway. -
Quantification of Polycyclic Aromatic Hydrocarbon in Standard
1 Polystyrene plastic: a source and sink for polycyclic aromatic hydrocarbons in the marine 2 environment 3 Chelsea M. Rochman1§, Carlos Manzano2§, Brian T. Hentschel1, Staci L. Massey Simonich2,3, 4 Eunha Hoh4* 5 6 1Department of Biology and Coastal and Marine Institute, San Diego State University, San 7 Diego, CA 8 2Department of Chemistry, Oregon State University, Corvallis, OR 9 3Department of Environmental and Molecular Toxicology, Oregon State University, 10 Corvallis, OR 11 4Graduate School of Public Health, San Diego State University, San Diego, CA 12 13 *Corresponding Author ([email protected]) 14 §Manzano and Rochman are equal contributors to the manuscript. 15 The current address for Chelsea Rochman is the Aquatic Health Program, University of 16 California, Davis, CA and for Carlos Manzano is the Canada Centre for Inland Waters, 17 Burlington, Ontario, Canada 18 Abstract 19 Polycyclic aromatic hydrocarbons (PAHs) on virgin polystyrene (PS) and PS marine 20 debris led us to examine PS as a source and sink for PAHs in the marine environment. At two 21 locations in San Diego Bay, we measured sorption of PAHs to PS pellets, sampling at 0, 1, 3, 6, 22 9 and 12 months. We detected 25 PAHs using a new analytical method with comprehensive two- 23 dimensional gas chromatography coupled to time-of-flight mass spectrometry. Several congeners 1 24 were detected on samples before deployment. After deployment, some concentrations decreased 25 (1,3-dimethylnaphthalene and 2,6-methylnaphthalene) while most increased (2-methylanthracene 26 and all parent PAHs (PPAHs) except fluorene and fluoranthene), suggesting PS debris is a 27 source and sink for PAHs. -
Pressure-Swing-Distillation Process for Separation of Tetrahydrofuran/Methanol
Pressure-Swing-Distillation Process for Separation of Tetrahydrofuran/Methanol Maradiya jay, Mehulkumar sutariya Sardar Vallabhbhai National Institute Of Technology, Surat Email: [email protected] Background Tetrahydrofuran (THF) is one of the most commonly used solvents in the chemical and the pharmaceutical industries due to its excellent dissolution ability. The production of steroid drugs faces the problem of separating solvent which contains THF and methanol. The separation and recycle of THF and methanol are of high economic significance and environmental importance. However, difficulty occur in the separation process because a minimum-boiling azeotrope is formed in the binary system. The pressure-swing-distillation (PSD) process, commonly used to separate azeotropic mixtures based on the shift of the relative volatilities and azeotropic compositions by changing the system’s pressure, is another suitable separation method for the separation of azeotropes. Efficient separation is achieved by two columns operating at two different pressure. Azeotropic data of Tetrahydrofuran/Methanol Figures: Effect of pressure on azeotropic composition and temperature. As shown in the figure, at atmospheric pressure (1 atm) azeotropic composition is near 45 mol% of Tetrahydrofuran and and 55 mol% Methanol. At 10 atm the azeotropic composition is changed to near 21 mol% of Tetrahydrofuran and 79 mol% of Methanol. Description of Flow-Sheet In this flow-sheet We use two distillation column with different pressure (1 atm and 10 atm). In low pressure column we enter a feed; This feed are concentrated near the azeotropic composition at 1 atm,and the 99.9 mol% Methanol are collected from the bottom. The top stream of low pressure column are now enter to the high pressure column where it’s composition are changed with the azeotropic composition at 10 atm, and the pure Tetrahydrofuran are collected from the bottom of that column and the top stream of high pressure column are recycled to the low pressure column.