Synthesis of Poly[Oligo(Hexafluoropropylene
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PTFE and PFA Similarities and Differences White Paper PTFE and PFA Similarities and Differences
White Paper PTFE and PFA Similarities and Differences White Paper PTFE and PFA Similarities and Differences Introduction The purpose of this document is to define and compare two of the most used fluoropolymers, PTFE and PFA, in industry globally and clarify the differences between them. Defining PTFE and PFA Polytetrafluoroethylene (PTFE) is a synthetic fluoropolymer of tetrafluoroethylene that has numerous applications. The most widely known PTFE formulation is sold under the brand name of Teflon®. PTFE was discovered by DuPont Co. in 1938. Perfluoroalkoxy alkanes (PFA) is a copolymer of hexafluoropropylene and perfluoroethers. It was developed after the discovery of PTFE by the same producer (DuPont Co.). One commonly known PFA formulation is Teflon PFA. PFA has very similar properties to PTFE, though the biggest difference between PTFE and PFA is that PFA is melt-processed. This is accomplished through conventional injection molding as well as screw extrusion techniques. Area of use PTFE is popularly used as a non-stick coating for pans and many modern items of cookware. PTFE is often used in containers and pipes for handling reactive and corrosive chemicals. This is because it has non-reactive properties. Another practical application of PTFE is as a lubricant. Used in this way, PTFE helps to reduce friction within machinery, minimize the “wear and tear,” and improve energy consumption. PFA is generally used for plastic lab equipment because of its extreme resistance to chemical attack, optical transparency, and overall flexibility. PFA is also often used as tubing for handling critical or highly corrosive processes. Other applications for PFA are as sheet linings for chemical equipment. -
Teflon™ FEP Fluoropolymer Resins
Teflon™ FEP Fluoropolymer Resins Product and Properties Handbook Teflon™ FEP Fluoropolymer Resins Table of Contents Introduction . 3 Commercially Available Products . 3 Specifications . 3 General Properties of Teflon™ FEP . 3 Typical Properties of Teflon™ FEP . 3 Mechanical Properties . 3 Tensile Properties . 4 Flexural Modulus . 4 Compressive Stress . 5 Creep and Cold Flow . 5 Apparent Modulus of Elasticity . 5 Stress Relaxation . 5 Poisson’s Ratio . 9 Fatigue Resistance . 9 Impact Resistance . 9 Hardness . 10 Friction . 10 Thermal Properties . 10 Electrical Properties . 11. Chemical Resistance . 11 Absorption . 11 Permeability . 11 Weathering . 11 Cryogenic Service . .11 Mildew Resistance . 13 FDA Compliance . 13 Optical Properties . 13 Fabrication Techniques . 13 Forming and Fabrication . 14 Choose Correct Working Speeds . 14 Properly Shape and Use Tools . 14 Rules for Dimensioning and Finishing . 15 Closer Tolerances . 15 Measuring Tolerances . 15 Surface Finishes . 15 Safety Precautions . 15 2 Teflon™ FEP Fluoropolymer Resins Introduction Specifications Teflon™ FEP (fluorinated ethylene propylene) is The ASTM material specification covering Teflon™ FEP chemically a copolymer of hexafluoropropylene fluoropolymer resin is D2116. Teflon™ FEP fluoropolymer and tetrafluoroethylene. It differs from PTFE resin is also called out in various industrial and military (polytetrafluoroethylene) resins, in that it is melt- specifications for tubing, molded parts, and film, as well as processible using conventional injection molding and numerous -
United States Patent (19) 11) Patent Number: 4,705,904 Bonfield Et Al
United States Patent (19) 11) Patent Number: 4,705,904 Bonfield et al. 45) Date of Patent: Nov. 10, 1987 54 VAPOR PHASE SYNTHESIS OF which comprises contacting in the vapor phase in a HEXAFLUOROSOBUTYLENE catalyst zone, B, of a reactor hexafluoropropylene oxide 75 Inventors: John H. Bonfield, Basking Ridge; with a fluorinated catalyst such as fluorinated silica Harry E. Ulmer, Morristown, both of alumina at a temperature of about 400-600 C. for a N.J. residence time sufficient to form a vapor stream com prising hexafluoroacetone which is thereafter directly 73) Assignee: Allied Corporation, Morris contacted in a heating zone of the reactor with a vapor Township, Morris County, N.J. stream comprising a keytone-generating compound 21 Appl. No.: 820,896 such as acetic anhydride at a temperature of about 500-700' C. for a residence time sufficient to form a 22 Filed: Jan. 17, 1986 stream comprising hexafluoroisobutylene, substantially free of perfluoroisobutylene and recovering the hexa Related U.S. Application Data fluoroisobutylene product is disclosed. A direct one 63 Continuation of Ser. No. 580,083, Feb. 14, 1984, aban reactor vapor phase synthesis of hexafluoroisobutylene doned. which comprises (a) contacting, in the vapor phase, 51) Int, Cl. .............................................. CO7C 17/26 hexafluoropropene with less than a stoichiometric 52 U.S. C. ..................................... 570/142; 570/153 amount of oxygen required to convert substantially all 58 Field of Search .................. 580/83; 570/153, 142; the hexafluoroisopropene into hexafluoropropylene 568/399, 407, 400, 384; 549/523 oxide in the presence of a fluorinated catalyst such as (56) References Cited fluorinated silica-alumina at a temperature of about 400-600 C. -
Catalytic Synthesis of Perfluorolyethers
J. Cent. South Univ. (2013) 20: 629-633 DOI: 10.1007/s1177101315285 Catalytic synthesis of perfluorolyethers YANG Weijun(阳卫军) 1, FANG Chao(方超) 1, ZHOU Jicang(周济苍) 2, GUO Cancheng(郭灿城) 1, WAN Wei(万伟) 2 1. College of Chemistry and Chemical Engineering, Hunan University, Changsha 410082, China; 2. Hunan Nonferrous Fluorine Chemistry Corporation, Changsha 410063, China © Central South University Press and SpringerVerlag Berlin Heidelberg 2013 Abstract: Perfluorolyether is characterized by highly chemical inertness, oxidative stability, anticorrosion as well as radiation resistance. It can be used as lubricant especially in harsh environmental conditions. In this work, hexafluoropylene oxide was catalytically polymerized at low temperature using the methods of anionic polymerization, and perfluorolyethers were obtained with numberaverage degree of polymerization more than 15. CsF and RbF were used as catalysts and their catalytic activities were investigated. Experimental results show that perfluorolyethers with numberaverage molar masses up to 3 000 g/mol could be obtained using the two kinds of catalysts, respectively. As compared to CsF, the numberaverage degree of polymerization is higher and the relative molecular mass distribution interval is narrower when RbF is used as catalyst. The effect of factors such as impurities’ content, reaction temperature and reaction time on the numberaverage degree of polymerization was also investigated. It is found that low impurities’ content and low temperature are beneficial to the generation of high numberaverage degree of perfluorolyethers. The optimization reaction time is 24 h, and further increase of reaction time does not significantly affect the average relative molecular mass. -
New Focus on Fep
NEW FOCUS ON FEP INTRODUCTION Since the fortuitous discovery and later commercialization of polytetrafluoroethylene, or PTFE, in the 1940’s, industry began to see the advantages of fluoropolymers. These polymer plastics are now almost synonymous with properties such as temperature and chemical resistance, abrasion protection, and generally excellent dielectric properties. After PTFE, manufacturers such as DuPont looked for other ways to expand upon commercially viable polymers containing fluorine. Work such as this lead to the fluoropolymer panorama of today. The most popular fluoropolymers generally fall into two groups: homopolymers, the result of polymerization – or combining – of identical monomers; and copolymers, polymerization incorporating two different monomers (Fig. 1). (Occasionally, commercially viable and useful fluoropolymers may even combine three different monomers). Fluorinated ethylene propylene, or FEP, falls into this second group. As a copolymer, FEP brings nearly all of the same preferred properties of the fluoropolymer “gold standard” PTFE but has several advantages. Fluoropolymers Homopolymers Copolymers PCTFE PVDF PTFE THV FEP ETFE ECTFE PFA (Terpolymer) Figure 1: Landscape of popular fluoropolymers. Homopolymers are produced through the polymerization of identical monomer units. Copolymers incorporate two or more monomers to produce the final polymer material. FEP is a copolymer. FEP SYNTHESIS AND STRUCTURE Introduced in 1960, FEP was the first copolymer made using TFE, the monomer used to synthesize PTFE. Instead of identical TFE monomers, FEP substitutes a –CF3 in place of one of the fluorine atoms of a TFE monomer changing it to hexafluoropropylene (HFP) (Fig. 2). Introducing the HFP monomer to PTFE reduces its ability to crystallize and reduces its melting point from 335 °C (635 °F) for PTFE to 260 °C (500 °F) for FEP. -
PTFE), Fluorinated Ethylene Propylene (FEP), Perfluoro- Alkoxy (PFA) and Ethylene-Tetrafluoroethylene (ETFE
http://www.e-polymers.org e-Polymers 2009, no 033 ISSN 1618-7229 Coating of Al mould surfaces with polytetrafluoroethylene (PTFE), fluorinated ethylene propylene (FEP), perfluoro- alkoxy (PFA) and ethylene-tetrafluoroethylene (ETFE) Akin Akinci,* Ebutalip Cobanoglu *Sakarya University, Faculty of Engineering, Department of Metallurgical and Materials Engineering, Esentepe Campus, 54187, Sakarya/Turkey; fax: +9026426955601; e-mail: [email protected] (Received: 23 October, 2008; published: 03 April, 2009) Abstract: Because of low cost, easily productivity and high thermal conductivity, aluminum (Al) moulds are preferred in the production of the polyurethane (PUR) parts. In this study, adhesion behavior and surface properties of coated materials between mould used in the production of automotive seat and PUR materials were investigated. Four different polymer types were coated on Al mould and they were characterized using contact angle, surface roughness, coating thickness, adhesion, cross-cut and SEM test methods. It was found that, PFA has the least value of surface roughness and ETFE has the highest one in the four different coatings produced. After holding period in isocyanate, decrease were measured on the angle values of all coatings. In the contact angle measurements before and after isocyanate tests, PFA exhibited the highest contact angle value. Introduction Polyurethanes (PURs) are used as flexible and rigid foams, elastomers and coatings. The term PUR is used to cover materials formed from the reaction of isocyanates and polyol. Flexible Polyurethane Foam (FPF) is mainly used in automotive industry as well as other various industries. Some problems can occur during the production process of FPF which are emanated by Reaction Injection Molding (RIM) process. -
C1-C4 Halogenated HC Info 16FEB2018.Xlsx
C1-C4 Halogenated Hydrocarbons/Halocarbons Not Otherwise Listed (C1-C4 NOL) Feb 28, 2018 Administrative Council Mtg - Printed 2/16/20184:11 PM Reported Uses (SOURCES:HAZMAP, NJDHSS, Wikipedia, TSCA CDR, mfr literature) TURA TSCA CDR Chemical CAS/Chemica chemical name chemical fire 2015 Chemical Name Pesti- blowing feedstock / supressant / propell- Inventory? TRI? List l Number (synonyms) formula Solvent refriger-ant etchant Other Tier II cide agent intermed-iate flame ant status* retardant insulation for refrigerators, freezers, commercial refrigeration equipment, refrigerated containers and LNG ships; spray foam insulation; insulated metal panels; slabstock and molded flexible foam; refrigerant for chillers; and solvents for metal cleaning and electronics, and circuit flush. https://www.honeywell-blowingagents.com/?document=solstice-lba-technical- HFO-1233zd (E) brochure&download=1 Hydro-fluoro-olefin C H ClF YYY yhttps://www.honeywell-refrigerants.com/americas/product/solstice-zd/ (HFO) 3 2 3 CDR 2016 Honeywell: 100% as propellants and blowing agents for plastics product mfg; R-1233zd CDR Honeywell Solstice® ZD refrigerant, Solstice® 1233zdE, Solstice Blowing Agent; Arkema (current Forane® 1233zd blowing agent for spray PU foam, appliance insulation, etc. and solvent (may Honeywell not be available in US) product) C1-C4 Cat 102687-65-0 1-Chloro-3,3,3-trifluoropropene Y 106‐95‐6 Allyl bromide 2-Propenyl bromide C3H5Br Y y Manufacture of synthetic perfumes, other allyl compounds; Insecticidal fumigant; 1-Propene, 3-bromo- Chemical intermediate in organic synthesis, for resins (copolymer with sulfur dioxide) and fragrances; As a fumigant (if quite volatile) or as a contact poison; C1-C4 Cat Used in the manufacture of plastics and dyestuff. -
Fluorinated Polymers
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract 94025 Process Economics Program Report No. 166 FLUORINATED POLYMERS (September 1983) This report deals with polytetrafluoroethylene (PTFE), and copolymers of tetrafluoroethylene with hexafluoropropylene, perfluoro- propylperfluorovinyl ether, and ethylene. For PTFE, both the suspen- sion process for making three grades (finely divided resin, presintered resin, and agglomerated resin), and the emulsion process for making coagulated resin and concentrated emulsion, are evaluated. SRI also evaluates the manufacture of the monomers for the above, viz., tetrafluoroethylene,hexafluoropropylene, perfluoropropylper- fluorovinyl ether. The last named monomer is made from perfluoro- .propionyl fluoride and hexafluoropropylene oxide; their manufacture is evaluated too. Also included in this report is a systematic study of fluorinated ion-exchange membranes which are made from a copolymer of tetrafluoro- ethylene and a perfluorinated vinyl ether with a carboxylic or sulfonic acid end group. The manufacture of perfluorinated vinyl ether, its copolymerization with tetrafluoroethylene to form an ion-exchange resin, and the processing of this resin to form a membrane, are all evaluated. PEP'83 YCY/CN Report No. 166 FLUORINATED POLYMERS by YEN-CHEN YEN with contributions by CHIEN NIEH and LIN CHAIO HSU I 0 1 September 1963 0E A private report by the m PROCESS ECONOMICS PROGRAM Menlo Park, California 94025 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLD PETROCHEMICALS Program covers major hydrocarbons and their derivatives on a worldwide basis. -
Fluoropolymers.Pdf
FLUOROPOLYMERS . General properties of fluoropolymers . Classification of fluoropolymers . Applying fluoropolymer coatings General properties of fluoropolymers Fluoropolymers are semicrystalline thermoplastics consisting of fluorinated olefinic monomers. Fluoropolymers contain fluorine (F) and their spesific properties result from the high energy bond C- F between the fluorine and carbon atoms. The higher the content of fluorine atoms in a polymer molecule, the stronger the spesific properties of the material. The properties of fluoropolymers: . Outstanding thermal stability. Some fluoropolymers can work continuously at temperatures as high as 554ºF (290ºC) and as low as -454ºF (-270ºC). Low coefficient of friction varying from 0.02 to 0.2 (depending on the fluoropolymer type, load and the sliding speed). Non-stick characteristics - poor adherence to other substances. Low surface energy (non-wetting). Fluoropolymers are hydrophobic and oleophobic - poorly wetable by both water and oils. Chemical inertness. Fluoropolymers are unaffected by most Solvents and other chemicals. Excellent dielectric properties such as electrical resistance, dielectric strength, low dissipation factor. Cryogenic stability. Classification of fluoropolymers There are two groups of fluoropolymers: homopolymers and copolymers . Homopolymers are polymers a molecule of which consists of a cain composed of repeatedly joined monomers: -A-A-A-...-A-. Polytetrafluoroethylene (PTFE) is a fully fluorinated polymer made by a polymerization of the monomer CF2=CF2 - tetrafluoroethylene (TFE). PTFE is one of the most widely used fluoropolymers due to its excellent properties: chemical inertness, low coefficient of friction (lower than 0.1), non-stick properties in a very wide temperature range. PTFE has a highest maximum service temperature 554ºF (290ºC). The main disadvantage of PTFE is very high viscosity in a molten state. -
Purification and Polymerization of Hexafluoropropylene Oxide
Europaisch.es Patentamf ® J) European Patent Office © Publication number: 0 062 325 A2 Office europeen des brevets EUROPEAN PATENT APPLICATION Application number: 82102822.2 © int.ci.»:C07D 303/48, C 07 D 301/32, C08G 65/22, C 08 G 65/32 Date of filing: 02.04.82 © Priority: 03.04.81 US 250905 © Applicant : E.I. DU PONT DE NEMOURS AND COMPANY, Legal Department 1007 Market Street, Wilmington Delaware 19898 (US) @ Date of publication of application : 1 3.1 0.82 Bulletin 82/41 Inventor: Darling, Thomas Robert, 203 Dakota Avenue, Wilmington Delaware 19803 (US) Representative: von Krelsler, Alek, Dipl.-Chem. et al, Designated Contracting States: BE DE FR GB IT NL Deichmannhaus am Hauptbahnhof, D-5000 Koln 1 (DE) @ Purification and polymerization of hexafluoropropylene oxide. Purified hexafluoropropylene oxide is produced by scrubbing to remove impurities that inhibit polymeriza- tion of hexafluoropropylene oxide, thus permitting the preparation of polymers having a degree of polymeriza- tion of more than 200, including end-capped and chain- extended derivatives thereof. Technical Field This invention relates to a method of purifying hexafluoropropylene oxide, to the purified product that results from that method, to the process of homopolymerization of said purified hexafluoro- propylene oxide, to the high molecular weight polymers that result from such homopolymerization, to the process of end-capping such high molecular weight polymers and the products that result from such process; and to the process of chain extending such high molecular weight polymers and the products that result from such process. The high molecular weight polymers of hexafluoropropylene oxide, including the end-capped and chain-extended derivatives thereof, are useful, depending on the molecular weight and various physical characteristics, as high performance elastomers, viscosity improvers for synthetic lubricants, or building blocks for preparing such viscosity improvers and high performance elastomers. -
Polymerization of Hexafluoropropylene Oxide
Europâisches Patentamt European Patent Office (JT) Publication number: 0154 297 Office européen des brevets B1 EUROPEAN PATENT SPECIFICATION @ Date of publication of the patent spécification: © int. ci - C 08 G 65/22, C 07 D 303/48 25.11.87 @ Application number: 85102221.0 (22) Date offilling: 02.04.82 @ Polymerization of hexafluoropropylene oxide. (30) Priority: 03.04.81 US 250905 (73) Proprietor: E.l. DU PONT DE NEMOURS AND COMPANY, 1007 Market Street. Wilmington Delaware 19898 (US) (43) Date of publication of application: 11.09.85 Bulletin 85/37 @ Inventor: Darling, Thomas Robert, 203 Dakota Avenue, Wilmington Delaware 19803 (US) @ Publication of the grant of the patent: 25.11.87 Bulletin 87/48 @ Représentative: von Kreisler, Alek, Dipl.- Chem., Deichmannhaus am Hauptbahnhof, D-5000 Kôln 1 @ Designated Contracting States: (DE) BEDE FRGBITNL (56) Références cited: FR-A-2 107 865 US-A-3 412 148 CÛ CM Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice to ^ the European Patent Office of opposition to the European patent granted. Notice of opposition shall be filed in a written reasoned yj statement. It shall not be deemed to have been filed until the opposition fee has been paid (Art. 99(1) European patent convension). LIBER, STOCKHOLM 1987 Technical Field This invention relates to a process of homopolymerization of purified hexafluoropropylene oxide, to the high molecular weight polymers that result from such homopolymerization, to the process of end-capping such high molecular weight polymers and the products that result from such process; and to the process of chain extending such high molecular weight polymers and the products that result from such process. -
Methods for Hexafluoroacetone Production
Journal content Methods for hexafluoroacetone production (1,1,1,3,3,3-hexafluoropropanone-2) T.E.Fiodorova Introduction For the first time hexafluoroacetone (HFA) was produced in 1941 by N.Fukuhara and L.A.Bigelow by direct fluorination of acetone. HFA is an extremely toxic reactive compound with the following main physical characteristics: Molecular mass 166.03 (1) Boiling point (760 mm of mercury column) 27.5oC Melting point -125.45 -129oC (1) Nonflammable HFA is an active electrophile and reacts with alkenes, ketenes, aromatic compounds, compounds containing active hydrogen atom etc. HFA does not form homopolymers but is readily copolymerized with various monomers to form chemically and heat resistant polymers. A field of HFA application is wide enough: production of solvents ( hexafluoroiso- propanol, for example), pharmaceuticals and agrochemicals, anticorrosive coatings, emulsifiers, dyes etc. 1.HFA production from acetone and its derivatives 1.1. HFA production by direct fluorination of acetone In 1941 N. Fukuhara and L.A.Bigelow reported about a process of gas-phase fluorination of acetone by fluorine-nitrogen mixture at different ratios of F2:CH3COCH3:N2. According to the authors, it was easy to fluorinate acetone in a reactor packed with copper gauze. The reaction products were separated and identified. The main reaction products were: HFA, monofluoroacetone, trifluoroacetyl fluoride, oxalyl fluoride, carbonyl fluoride and tetrafluoromethane. The fraction (b.p. -35- -16oC) containing HFA was separated in amount of 5-10% of the whole liquid volume (4). The reaction of direct fluorination is dangerous and difficult to control, therefore this method was not spread widely but it is still of interest.