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119 results about "Dichlorodifluoromethane" patented technology

Dichlorodifluoromethane (R-12) is a colorless gas usually sold under the brand name Freon-12, and a chlorofluorocarbon halomethane (CFC) used as a refrigerant and aerosol spray propellant. Complying with the Montreal Protocol, its manufacture was banned in developed countries (non-article 5 countries) in 1996, and developing countries (article 5 countries) in 2010 due to concerns about its damaging effect on the ozone layer. Its only allowed usage is as fire retardant in submarines and aircraft. It is soluble in many organic solvents. Dichlorodifluoromethane was one of the original propellants for Silly String. R-12 cylinders are colored white.

Power generation system for waste heat of medium and low temperature flue gas with heat pipe heat exchanger organic medium Rankine cycle

The invention provides a power generation system for waste heat of medium and low temperature flue gas with heat pipe heat exchanger organic medium Rankine cycle, and belongs to the technical field of energy and environment. The invention comprises a heat pipe heat exchanger system, a working medium circulation loop of organic Rankine cycle, a medium and low temperature flue gas exhausting pipeline, a heating hot water loop and a cooling water loop, wherein an ascending pipe and a descending pipe of a boiler are replaced by heat pipes, the heat pipe heat exchanger system is formed by a heat pipe, a flue gas heat exchanger and a boiler cylinder, evaporating section of the lower end of the heat pipe is arranged in flue gas heat exchanger, condensing section of the upper end is arranged in the boiler barrel, toluene, dichlorodifluoromethane, propane and pentafluoropropane are used as working medium, 20% volume of the softening desalted water is used as the heat pipe fluid. The invention has advantages of high efficiency of heat exchange, convenient replacement of heat pipe, being capable of avoiding corrosion and uneasy-change of the heat exchanger pipe, affecting the heat transfer efficiency and leakage of the working medium and other advantages, and being capable of adjusting exhaust heat of the organic Rankine cycle according to the demand for heating load of users.
Owner:KUNMING UNIV OF SCI & TECH

Refrigeration compressor lubricant

Disclosed are working fluid compositions for heat transfer apparatuses, such as refrigeration systems, that include a refrigerant and an ester based lubricant. The working fluid may comprise ≦50% by weight of the ester based lubricant composition and ≧50% by weight of one or more refrigerant compounds. The ester based lubricant comprises an additive selected from the group consisting of: diaryl sulfides, arylalkyl sulfides, dialkyl sulfides, diaryl disulfides, arylalkyl disulfides, dialkyl disulfides, diaryl polysulfides, arylalkyl polysulfides, dialkyl polysulfides, dithiocarbamates, derivatives of 2-mercaptobenzothiazole, derivatives of 2,5-dimercapto-1,3,4-thiadiazole, and combinations thereof. The refrigerants may be C3-C8 hydrocarbons, trichlorofluoromethane (CFC-11), dichlorodifluoromethane (CFC-12), saturated hydrofluorocarbons, difluoromethane (HFC-32), 1,1,2,2-tetrafluoroethane (HFC-134), difluoroethane (HFC-152a), fluoroethane (HFC-161), R410A (a near-azeotropic mixture of difluoromethane (HFC-32) and pentafluoroethane (HFC-125)), 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea), 1,1,1,2,3,3-hexafluoropropane (HFC-236ea), 1,1,1,3,3,3-hexafluoropropane (HFC-236fa), 1,1,1,3,3-pentafluoropropane (HFC-245fa), 1,1,1,3,3-pentafluorobutane (HFC-365mfc), hydrofluoroolefins, dimethyl ether, carbon dioxide, bis(trifluoromethyl)sulfide, and trifluoroiodomethane and combinations thereof.
Owner:COPELAND LP

Bio-safety disposal method for dispelling dichlorodifluoromethane by induction heating and pyrolysis induction heating furnace

The invention relates to a bio-safety disposal method for dispelling dichlorodifluoromethane by induction heating and a pyrolysis induction heating furnace. The method is characterized by comprising steps of carrying out pyrolytic reaction on a preheated feed gas which is a mixed gas of dichlorodifluoromethane, steam and air in a high-temperature environment generated by induction heating and carrying out absorption and inversion on pyrolysis products, wherein the proportioning of the feed gas is as follows: the flow ratio of the steam to the dichlorodifluoromethane is shown in the specification, the flow ratio of the air to the dichlorodifluoromethane is shown in the specification, and in the formula, a, b and c are respectively the number of carbon, hydrogen and halogen atoms of one dichlorodifluoromethane molecule. The pyrolysis induction heating furnace is characterized in that a crucible in the traditional pyrolysis induction heating furnace is internally provided with an acid corrosion resistant and thermostability bending-shaped metal coiler, the supply frequency is 10-300kHz and the power is 10-50kW. The invention has the advantages of quick warming speed, little power consumption, high energy utilization rate and pyrolysis efficiency, convenient starting operation, good operation safety and easy scale realization.
Owner:TIANJIN HEJIA VEOLIA ENVIRONMENTAL SERVICES

A kind of preparation method of trifluoroethylene and tetrafluoromethane

The invention relates to a preparation method for trifluoroethylene and tetrafluoromethane. The method is characterized in that: dichlorodifluoromethane and 1,1,1,2-tetrafluoroethane are mixed according to a mole ratio of the dichlorodifluoromethane to the 1,1,1,2-tetrafluoroethane of 1:2-9, and are subjected to a reaction at a temperature of 350-500 DEG C and space velocity of 700-1500 hour<-1> under normal pressure through a catalytic action of a fluorination catalyst; the resulting end gas is separated through a partition column I; the separated dichlorodifluoromethane, the separated fluoride hydrogen and the separated 1,1,1,2-tetrafluoroethane are separated through a partition column II, wherein the resulting dichlorodifluoromethane and the resulting 1,1,1,2-tetrafluoroethane are recycled, the resulting fluoride hydrogen is adopted as the by-product to be collected; the separated trifluoroethylene and the separated tetrafluoroethane are subjected to separation through a partition column III, and purification to obtain the pure trifluoroethylene and the pure tetrafluoroethane. The preparation method provided by the present invention has characteristics of low reaction temperature, low energy consumption and less damage to the equipment.
Owner:ZHEJIANG NORMAL UNIVERSITY +1

Method for producing tetrafluoromethane by gas phase catalysis

The invention discloses a method for producing a tetrafluoromethane by gas phase catalysis. Aiming at the defects of high needed reaction temperature and low conversion per pass existing in the conventional process for producing FC-14 by gas phase fluorination, the invention provides an economic and high-efficient method for producing the tetrafluoromethane by gas phase catalysis, which has the advantages of low needed reaction temperature and high conversion per pass. The method for producing the tetrafluoromethane comprises the following step: reacting halohydrocarbon with hydrogen fluoride at the presence of a gas phase fluorination catalyst in a gas phase to produce the tetrafluoromethane, wherein the molar ratio of the halohydrocarbon to the hydrogen fluoride is 1:1-10; the halohydrocarbon is one or more of the tetrafluoromethane, trichloromonofluomethane, dichlorodifluoromethane and monochlorotrifluoromethane; the used gas phase fluorination catalyst adopts a chromium compound as an active component and an aluminum compound as a carrier; and the molar ratio of the chromium to the aluminum is 1:1-19. The method for producing the tetrafluoromethane has the characteristics of long service life and high percent conversion of the halohydrocarbon.
Owner:ZHEJIANG NORMAL UNIVERSITY +1

Synthesizing method for 2,2-difluoro-1,3-benzodioxole

The invention relates to a synthesizing method for 2,2-difluoro-1,3-benzodioxole. The method comprises the steps that 1, sodium hydroxide and water are added into a reaction kettle, then liquid paraffin is added, the temperature is increased to control the temperature of the reaction kettle to be under the condition of 85 DEG C, pyrocatechol is added, the temperature is kept at 85 DEG C, reacting is performed for 1 hour, and then pyrocatechol sodium salt is prepared; 2, methylbenzene, water and catalysts are added in a high-pressure kettle, the high-pressure kettle is closed, replacement is performed for three times with nitrogen, the temperature is increased to control the temperature of the high-pressure kettle to be under the condition of 95 DEG C, the pyrocatechol sodium salt prepared in the step 1 and dichlorodifluoromethane are added, the pyrocatechol sodium salt is preheated to 85 DEG C-90 DEG C in advance before being fed, the temperature of the high-pressure kettle is kept at 95 DEG C-105 DEG C, reacting is performed for 1 hour, the high-pressure kettle is cooled to 20 DEG C, an organic layer solution is separated out, washing is performed for one time, the organic layer solution is rectified to collect rectified components, and the 2,2-difluoro-1,3-benzodioxole is obtained. The synthesizing method for the 2,2-difluoro-1,3-benzodioxole has the advantages of being simple and direct in technology, few in technology waste materials, high in yield and suitable for large-scale industrialized production.
Owner:JIANGSU REPONT PESTICIDE FACTORY
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