Abstract:
PROBLEM TO BE SOLVED: To provide a method for producing a monomer for vinylidene fluoride (VDF)-based curable fluoroelastomers having a glass transition temperature of lower than -35°C and an amount of -COF end groups in the polymer of not higher than the sensitivity limit of the method using FT-IR spectroscopy.SOLUTION: The method for producing the monomer CFOCFOCF=CF(a) comprises reacting CFOF with CO to obtain fluoroformate CFOCOF, reacting the fluoroformate with elemental fluorine and an olefin compound having the formula: CAF=CA'F (wherein A and A' are the same or different and are H, Cl or Br with proviso that both are not H) to obtain a fluorohalogen ether of the formula: CFOCFOCFACFA' (wherein A and A' are the same as defined above), and removing the substituents A and A' from the fluorohalogen ether.
Abstract:
PROBLEM TO BE SOLVED: To provide a heat exchange liquid or a hydraulic liquid that does not have an adverse affect on the ozone layer, does not have the neutron moderation effect under ionizing radiation or neutron irradiation, and does not exhibit induced radiation phenomena. SOLUTION: In a method of exposure of ionizing radiation and/or neutron irradiation using a circulation passage or a device, a fluorinated compound selected from hydrofluoroethers is used as a heat exchange liquid or a hydraulic liquid in the circulation passage or device. The fluorinated compound is selected from hydrofluoroethers which are liquid under indoor conditions (25°C and 1 atmospheric pressure). COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide non-combustible polyesterpolyol and/or polyetherpolyol premix for producing a foamed product. SOLUTION: The premix comprises a polyol, 4% by mass or more of a binary foaming agent mixture of HFC 365 mfc and an additional fluorocarbon and 10 to 20% by mass of a phosphor-based flameproofing agent. COPYRIGHT: (C)2009,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide an assembly or an MEA device in which not only coolant fluid having a lower purity than required in a conventional technology can be used, but also coolant fluid formed from a mixture of water and a high-boiling-point solvent can be used, and an adhesion of a sub-gasket with an MEA lasts long. SOLUTION: The assembly or the MEA device is composed of a membrane and two electric catalyst layers on both sides of the membrane. Each area of the two electric catalyst layers is smaller than that of the membrane. On each of both sides of an ionomer membrane, at least one sub-gasket is arranged in a non-catalyst area of the MEA and an edge of the ionomer membrane is sealed between the sub-gaskets. COPYRIGHT: (C)2007,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a catalyst coated membrane, in which the dimension variation in a hydration/dewater cycle is reduced, the adhesion of an ionomer-membrane with an electrode catalyst layer is improved, the adhesion between catalyst coated membrane layers after an immersion cycle does not vary, and the stability of the improved catalyst coated membrane in an electrochemical battery is held. SOLUTION: The catalyst coated membrane is a membrane having a first electrode catalyst layer containing a catalyst in one plane in two surfaces, and a second electrode catalyst layer containing a catalyst in the other plane. The electrode catalyst layer and the membrane contain (per)fluorinated ionomer. The dimension of the catalyst coated membrane varies not larger than 15% in the perpendicular direction of the xy plane thereof after the catalyst coated membrane is immersed in a desalted water at 100°C for 30 minutes then dried in vacuum at 105°C for 1 hour. The dimension does not vary after immersing in water at 80°C for 8 hours and followed by 60 cycles of immersion in water at 25°C for 16 hours. COPYRIGHT: (C)2006,JPO&NCIPI
Abstract:
PROBLEM TO BE SOLVED: To provide a method for producing peroxide of a perfluoropolyether producing commercial perfluoropolyether product without using a CFC-12 solvent. SOLUTION: The invention relates to the method for producing peroxide of perfluoropolyether comprising photooxidation of TFE in the presence of a UV-light and in presence of a mixture of solvent formed from HFC-227 and a solvent selected from HFC-125 and HFC-218 at -80 to -40°C, obtaining the peroxide with ≥1.2 of peroxide content represented by the formula: A-CF 2 O(CF 2 CF 2 O) m (CF 2 O) n -(CF 2 CF 2 OO) m1 (CF 2 OO) n1 CF 2 -B, [in the formula A and B are each the same or different -Cl, -F, -F 2 CCl, -COF, -OCOF, -CF 3 and m, m1, n and n+1 are each an integer satisfying 0.9
Abstract:
PROBLEM TO BE SOLVED: To provide a perfluoroelastomer composition which has improved heat resistance at high temperatures even up to 350°C, preferably up to 340°C. SOLUTION: The crosslinking system for perfluoroelastomers hardenable by a peroxidizing process comprises a bis-olefin expressed by general formula (1) [wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are each the same or different H, or a 1-5C alkyl group; Z is a 1-18C straight- or branched-chain alkylene or cycloalkylene group or a (per)fluoropolyoxyalkylene group, each of which may contain optionally an oxygen atom] as a crosslinking agent the amount of which is 0.6-1.8 wt.% in the whole polymer, and such a peroxide for use in the peroxide hardening as is capable of producing a radical by heating and as is in an amount of 0.2-1.3% by weight relative to the polymer. COPYRIGHT: (C)2006,JPO&NCIPI
Abstract:
PROBLEM TO BE SOLVED: To provide a fluoropolymer dispersion liquid that does not practically contain a fluorinated anionic surfactant, can be produced continuously or discontinuously with a high industrial productivity, and can be filtered within a very short time through an 80 μm net and subsequently through a 10 μm net, preferably does not leave behind any coagulated matter on the 10 μm net. SOLUTION: The method for producing a fluoropolymer dispersion liquid that does not practically contain a fluorinated anionic surfactant comprises the following processes: (a) a 1.5-25 wt% nonionic surfactant against a weight of a fluoropolymer contained in a fluoropolymer dispersion liquid is added to the dispersion liquid, (b) to the dispersion liquid is added a water soluble salt that does not give any precipitate in the dispersion liquid in a operating condition, (c) the dispersion liquid is contacted with a basic anionic ion-exchange resin and then (d) the dispersion liquid is separated from the basic anionic ion-exchange resin, wherein the dispersion liquid is to be filtered before the process (d) through a 180 μm net and successively through a 10 μm net. COPYRIGHT: (C)2005,JPO&NCIPI