145 results about "Trifluoroethane" patented technology

A binary refrigerating apparatus employs a refrigerant composition that has a small global-warming potential (GWP) to be earth friendly, can be used as a refrigerant capable of achieving a low temperature of −80° C., and is excellent in refrigerating capacity and other performance. A refrigerant composition used as a low-temperature-side refrigerant is a refrigerant mixture including a non-azeotropic mixture in which 20% by mass or less of carbon dioxide (R744) is mixed to difluoroethylene (R1132a). A refrigerant composition used as a high-temperature-side refrigerant is a combination of: a non-azeotropic mixture comprising the refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a) and 1,1,3-trifluoro ethane (R143a); and 1,1,1,2,3-pentafluoropentene (HFO-1234ze), having a global-warming potential (GWP) of 1500 or less.

The present invention relates to a refrigerant mixture for substituting R502, R22 or R12 used in a vapor compression refrigerator or air conditioner and a refrigeration system using the same. More specifically, the present invention relates to a refrigerant mixture comprising a combination of two or three components, which is capable of being used without causing ozone layer destruction and global warming and at the same time, without replacement of the existing refrigeration system, wherein the components are selected from the group consisting of propylene, propane, 1,1,1,2-tetrafluoroethane, pentafluoroe thane, 1,1,1-trifluoroethane, 1,1-difluoroethane, dimethylether and isobutane; and a refrigeration system using the same.

A dry etching method wherein a resist film is irradiated with radiation having a wavelength of not more than 195 nm to form a resist pattern having a minimum line width of not more than 200 nm, and the substrate having the resist pattern formed thereon is subjected to dry etching using a fluorine-containing compound having 4 to 6 carbon atoms and at least one unsaturated bond as an etching gas. As the fluorine-containing compound, perfuloro-2-pentyne, perfuloro-2-butyne, nonafluoro-2-pentene and perfluoro-2-pentene are preferably used. Perfuloro-2-pentyne is produced by a process wherein a 1,1,1-trihalo-2,2,2-trifluoroethane is allowed to react with pentafluoropropionaldehyde to give a 2-halo-1,1,1,4,4,5,5,5-octafluoro-2-pentene, and the thus-produced halo-octafluoro-2-pentene is dehydrohalogenated.

The invention relates to a non-combustible mixing refrigerant suitable for deep refrigeration temperature of minus 80 DEG C to minus 100 DEG C. The non-combustible mixing refrigerant comprises five groups of materials, where the first group of material is tetrafluoromethane; the second group of material is trifluoromethane, hexafluoroethane or a mixture of the trifluoromethane and the hexafluoroethane; the third group of material is pentafluoroethane, trifluoroethane, perfluoropropane, difluoromethane or a mixture of two, three or multiple of the pentafluoroethane, the trifluoroethane, the perfluoropropane and the difluoromethane; the fourth group of material is iodotrifluoromethane, 1, 1, 2, 2-tetrafluoroethane, 1,1-difluoroethane, 2, 3, 3, 3-tetrafluoropropene, 1, 3, 3, 3-tetrafluoropropene or a mixture of two, three or multiple of the iodotrifluoromethane, the 1, 1, 2, 2-tetrafluoroethane, the 1,1-difluoroethane, the 2, 3, 3, 3-tetrafluoropropene and the 1, 3, 3, 3-tetrafluoropropene; the fifth group of material is perfluoro-n-butane, 1, 1, 1, 3, 3-perfluoropropane or a mixture of the perfluoro-n-butane and the 1, 1, 1, 3, 3-perfluoropropane; the molar concentrations of the five groups of materials are respectively 25-50%, 15-40%, 10-30%, 5-20% and 10-25%; and the non-combustible mixing refrigerant is safe in a back-heating type throttling refrigeration system, can realize the refrigeration in the temperature range of minus 80 DEG C to minus 100 DEG C and has low whole green house effect without ozone depletion effect.

The multicomponent mixed work medium throttling refrigerating agent applicable to 200-240 k temp. zone includes four groups of substances, respectively are: first group includes tetrafluoromethane, nitrogen trifluoride or mixture; second group includes ethylene, ethane, fluoroform, xenon, fluromethane, perfluoroethylene, fluoroethylene, perfluoroethane or their any two, three and several kinds or mixture of all them; fourth group includes 1-butylene, isobutane, 2-methyl butane, 1-pentene, 3-methyl-1-butylene, 2-methylpentane, 2-butylene, cyclobutane, isobutylene, n-butane, pefluorobutane, n-pentane, perfluoropentane or their two, three, several kinds ormixture of all the them; and third group includees propylene, propane, perfluoropropane, 1,1,1-trifluoroethane, 1,1,-bifluoroethane.

A process for producing 1,1,1,2,2-pentafluoroethane by fluorinating with hydrogen fluoride at least one of 2,2-dichloro-1,1,1-trifluoroethane and 2-chloro-1,1,1,2-tetrafluoroethane as a starting material, the process being characterized by separating the reaction mixture resulting from the fluorination into a product portion A mainly containing 1,1,1,2,2-pentafluoroethane and a product portion B mainly containing 2,2-dichloro-1,1,1-trifluoroethane, 2-chloro-1,1,1,2-tetrafluoroethane and hydrogen fluoride, removing a fraction mainly containing 2,2-dichloro-1,1,1,2-tetrafluoroethane from the product portion B, and recycling the rest of the product portion B as part of feedstocks for fluorination.According to the process of the invention, the amount of CFC-115 contained in the target HFC-125 can be remarkably reduced through a simplified procedure.

The invention discloses a method of preparing the pentafluoroethane (HFC-125), which adopts the hydrogen fluoride (HF) and the perchlorethylene (PCE) as the material, and takes two reactors and two steps of gas phase catalysis fluorination reaction. A first reactor fluorinates the PCE and synthesizes 2,2-dichlor-1,1,1-trifluoroethane(HCFC-123) and 2-chlorin-1,1,1,2-tetrafluorothane(HCFC-124), and the second reactor fluorinates HCFC-123 and HCFC-124 and synthesizes HFC-125. The unreacted PCE in the resultant flow of the first reactor is separated by a first distillation tower and then circulates to the first reactor; the HF, HCFC-126, HCFC-124, HFC-125 and HCL in the resultant flow of the first reactor and the second reactor are separated by a second distillation tower and a third distillation tower, and then the separated HF circulates to the first reactor and the second reactor, while the HCFC-123, the HCFC-124 and the HFC-134a circulate to the second reactor. The invention can prolong the service life of the catalyst and improve the one-way conversion of PCE as well as remarkably reduce the content of chloropentafluoroethane(CFC-115) in the desired product HFC-125.

Refrigerant compositions include mixtures of difluoromethane and isobutane, butane, propylene or cyclopropane; pentafluoroethane and propylene or cyclopropane; 1,1,2,2-tetrafluoroethane and propane; 1,1,1,2-tetrafluoroethane and cyclopropane; 1,1,1-trifluoroethane and DME or propylene; 1,1-difluoroethane and propane, isobutane, butane or cyclopropane; fluoroethane and propane or cyclopropane; 1,1,1,2,2,3,3-heptafluoropropane and butane, cyclopropane, DME, isobutane or propane; or 1,1,1,2,3,3,3-heptafluoropropane and butane, cyclopropane, isobutane or propane.

A novel refrigerant composition useful as a substitute for HCFC-22, comprising a first constituent of difluoromethane (CH2F2, HFC-32); a second constituent of pentafluoroethane (CHF2CF3, HFC-125); a third constituent of 1,1,1-trifluoroethane (CH3CF3, HFC-143a); a fourth constituent selected from the group consisting of cyclopropane (C3H6, RC-270), 1,1,1,2,3,3,3-heptafluoropropane (CF3CHFCF3, HFC-227ea), 1,1,1,2,2-pentafluoropropane (CH3CF2CF3, HFC-245cb), isobutane (CH(CH3)2CH3, R-600a), octafluorocyclobutane (C4F8, RC-318), 1,1,1,2,3,3-hexafluoropropane (CHF2CHFCF3, HFC-236ea), butane (C4H10, R-600), bis(difluoromethyl)ether (CHF2OCHF2, HFE-134) and pentafluoroethylmethylether (CF3CF2OCH3, HFE-245).

The invention discloses a method for preparation of trifluoro acetyl chloride with trifluoroethane chlorinated mixture, which comprises the following steps: 1) adding trifluoroethane chlorinated mixture into a reactor, continuously introducing oxygen and chlorine under stirring, irradiating with a mercury lamp for photochemical oxidation, continuously discharging reactants in the form of gas phase from the upper part of the reactor, and continuously supplementing the trifluoroethane chlorinated mixture to maintain the level in the reactor constant; and 2) condensing the gasified trifluoroethane chlorinated mixture in the reactor through a condensation and separation tower and making the condensed trifluoroethane chlorinated mixture return to the reactor to continuously react, discharging the product trifluoro acetyl chloride from the top of the condensation and separation tower and collecting the trifluoro acetyl chloride after compression and condensation. Compared with the existing preparation method, the invention has the advantages that: the trifluoroethane chlorinated mixture can be directly used for preparation of the trifluoro acetyl chloride without separation, the processis advanced and reasonable, the synthesis route is simplified, the time is reduced, the production efficiency is greatly enhanced, and the equipment investment and energy consumption are reduced.

Methods and systems for liquefying natural gas using nonflammable refrigerants are provided. Methods of liquefaction include cooling a natural gas stream via indirect heat exchange with a first nonflammable refrigerant selected from the group consisting of: difluoromethane, pentafluoromethane, trifluoromethane, hexafluoroethane, tetrafluoroethane, pentafluorethane, trifluoroethane, pentafluoroethane, any derivative thereof, and any combination thereof during a first refrigeration cycle; and cooling the natural gas stream via indirect heat exchange with a second refrigerant during a second refrigeration cycle.

A process is disclosed for making 1,1,1,4,4,4-hexafluoro-2-butene. The process involves reacting 2,2-dichloro-1,1,1-trifluoroethane with copper in the presence of an amide solvent and 2,2′-bipyridine. A process is also disclosed for making 1,1,1,4,4,4-hexafluoro-2-butene. The process involves reacting 2,2-dichloro-1,1,1-trifluoroethane with copper in the presence of an amide solvent and a Cu(I) salt. A process is further disclosed for making 1,1,1,4,4,4-hexafluoro-2-butene. The process involves reacting 2,2-dichloro-1,1,1-trifluoroethane with copper in the presence of an amide solvent, 2,2′-bipyridine and a Cu(I) salt.

The present invention discloses one kind of multicomponent mixture work medium suitable for fractional condensation type heat pump circulation system. The mixture work medium or mixed refrigeratant consists of two components, including one low boiling point component and one high boiling point component. The low boiling point component is one or several selected from difluro methane, trifluoro ethane, fluoro ethane, propylene, propane, pentafluoro ethane, etc. The high boiling point component is one or several selected from isobutane, n-butane, butene, isobutene, octafluoro isobutene, octafluoro cyclobutane, etc.

The invention relates to a liquid-phase reaction preparation method of fluorides. The liquid-phase reaction preparation method comprises the following steps: raw material mixing: mixing a potassium fluoride water solution and CHF2CH2Cl according to the weight ratio of (1-10): 1, wherein the concentration of the potassium fluoride water solution is 1%-6%; reaction: performing chemical reaction on the mixed raw materials, wherein the reaction temperature is 80-360 DEG C, the reaction pressure is 0.1-25MPa, and the reaction retention time is 10-90min; cooling, and receiving the materials so as to obtain trifluoroethane and difluoroethanol. According to the liquid-phase reaction preparation method of the fluorides, provided by the invention, the one-time yield of difluoroethanol can achieve 30-60%, and the one-time yield of trifluoroethane can achieve 5-25%.

A process for preparing 1,1,1-trifluoroethane (HFC-143a) features the gas-phase reaction between HF and 1,1,1-trichloroethane (HCC-140a) under the existence of fluorinating Cr-base catalyst at 150-280 deg.C. It has high output rate and selectivity.

The multicomponent mixed work medium throttling refrigerating agent applicable to medium-low temp. zone includes five groups of substances, the sum of their mole concentration is 100%, in which first group includes methane, krypton or mixture, total mole concentration is 5%-45%, second group includes tetrafluoromethane, nitrogen trifluoride or mixture, total mole concentration is 15%-55%; fourth group includes propylene, propane, perfluoropane, 1,1,1-trifluoroethane, 1,1-bifluoroethane, fluoroethane, propadiene, cyclopropane, or mixture, total mole concentration is 5%-25%; fifth group includes 1-butylene, isobutane, 2-methylbutane, 1-pentene, 3-methyl-1-butylene, 2-methylpentane, 2-butylene, isobutylene, n-butane, perfluorobutane, n-pentane or mixture, total mole concentration is 5%-25%.

The invention discloses an N-bisbenzenesulfonyl-1-phenylseleno trifluoroethane derivative synthesis method, which comprises: carrying out a one-step reaction by using a diazo compound, a diether compound and N-fluorobisbenzenesulfonyl imide as raw materials and using an organic solvent as a solvent in the absence of a catalyst to obtain the N-bisbenzenesulfonyl-1-phenylseleno trifluoroethane derivative. According to the invention, the synthesis method has efficient atom economy, does not need any organic catalysts or metal catalysts, and is simple and safe to operate, and the synthesized N-bisbenzenesulfonyl-1-phenylseleno trifluoroethane derivative is an important organic synthesis and medical intermediate.

The invention discloses a mixed working medium for an organic working medium rankine cycle system of a screw expander. The mixed working medium consists of two or three of four organic working media, namely HCFC(hydrochlorofluorocarbon)-123 (2,2-dichloro-1,1,1-trifluoroethane), HFC(hydro-fluoro-carbon)-245fa (1,1,1,3,3-pentafluoropropane), HFC-152a (1,1-difluoroethane) and HFC-134a (1,1,1,2-tetrafluoroethane). The sum of mass percentage of components of each mixed working medium is 100 percent. The preparation method for the mixed working medium comprises the following step of: physically mixing the components in the set mass ratio at normal temperature. The mixed working medium meets environmental protection requirement, namely has the ozone depletion potential (ODP) of zero, low global warming potential (GWP), suitable thermal parameters, good cycle performance and high cycle heat utilization rate.

The invention discloses a preparation method of hexafluorobutadiene. The preparation method includes the following steps that (1) a hydrogenation reaction is carried out with trifluorochlor oethyleneas raw materials under the action of a first catalyst to obtain trifluoroethylene; (2) the trifluoroethylene is introduced into a bromination reactor for conducting a bromination reaction with brominein the reactor, 1,2-dibromo-1,1,2-trifluoroethane is obtained, and then trifluorobromoethylene is obtained by dehydrobromination; (3) the trifluorobromoethylene reacts in a reactor containing a solvent, an initiator and zinc powder to generate zinc reagent trifluorovinyl zinc bromide; and (4) the zinc reagent trifluorovinyl zinc bromide is coupled under the action of a second catalyst to obtain the hexafluorobutadiene. The preparation method has the advantages of low energy consumption, high yield, high reaction efficiency and the like.

The invention discloses a method for preparing trichloroethylene, which is characterized in that: with the existence of organic solvent, 1,1,2-tribromo trifluoroethane is adopted to be reacted with metal dehalogenating agent to generate metallorganics of trichloroethylene-base bromide, then water is dropped into the metallorganics to obtain trichloroethylene gas, the metal dehalogenating agent is metal zinc powder or metal magnesium powder, and the organic solvent is nonprotonic polarity polar solvent. The product produced through the method has high selectivity and is easy to separate and purify.

In accordance with the present invention a composition is provided. The composition comprises Z-1,1,1,4,4,4-hexafluoro-2-butene (Z-HFO-1336mzz) and 2,2-dichloro-1,1,1-trifluoroethane (HCFC-123). Also in accordance with the present invention a method is provided for topping-off or replenishing a refrigerant charge. The method comprises adding a second refrigerant to a refrigeration, air conditioning, heat pump or power cycle system containing HCFC-123 as a first refrigerant, wherein said second refrigerant comprises Z-HFO-1336mzz and optionally HCFC-123, thus producing a refrigerant composition comprising the first refrigerant and the second refrigerant. Also in accordance with the present invention another method is provided. The method comprises replacing HCFC-123 in a refrigeration, air conditioning, heat pump or power cycle system with a refrigerant composition comprising Z-HFO-1336mzz and optionally HCFC-123.

The invention discloses a preparation method of a 2,4-dichloro-1,1,1-trifluorobutane derivative. The 2,4-dichloro-1,1,1-trifluorobutane derivative is prepared by taking 2,2-dichloro-1,1,1-trifluoroethane and CH2=CHR as raw materials in the presence of a polymerization regulating catalyst, a catalytic promoter and a solvent, wherein the polymerization regulating catalyst is copper chloride or cuprous chloride, the catalytic promoter is 2,2-dipyridyl, pentamethyl diethylenetriamine, tri(2-pyridyl methyl) amine or tri(2-dimethylamino ethyl) amine, the solvent is acetonitrile, methyl alcohol or dimethyl sulfoxide. The invention provides a novel synthesis route which produces less three wastes and is high in catalytic efficiency, and is mainly used for preparing the 2,4-dichloro-1,1,1-trifluorobutane derivative.