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188 results about "Fluoroform" patented technology

Fluoroform is the chemical compound with the formula CHF₃. It is one of the "haloforms", a class of compounds with the formula CHX₃ (X = halogen) with C₃ᵥ symmetry. Fluoroform is used in diverse applications in organic synthesis. It is not an ozone depleter but is a greenhouse gas.

Non-combustible mixing refrigerant suitable for deep refrigeration temperature of minus 80 DEG C to minus 100 DEG C

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.
Owner:中科赛凌(北京)科技有限公司

Method and device for refining chlorine hydride byproduct and recovering trifluoromethane in production of monochlorodifluoromethane

The invention relates to a method for refining a chlorine hydride byproduct and recovering trifluoromethane in production of monochlorodifluoromethane. Refined high-purity chlorine hydride can directly serve as a raw material for synthesizing vinyl chloride monomers; and the trifluoromethane byproduct separated in the refining process can be effectively recovered, wherein the refining of the HCl comprises the following steps of: crude separation, absorption, analysis, condensation, capture of acid mist, and adsorption; and after a F23 byproduct in the production of the monochlorodifluoromethane is separated in the absorption process in the refining of the HCl, the F23 byproduct is subjected to lossless compression and rectification to form the trifluoromethane with the purity of over 99 vol percent. By combining the recovery and comprehensive utilization of the HCl and the recovery of the trifluoromethane, the high consumption of water resources and liquid caustic soda is avoided, and the production cost of the monochlorodifluoromethane is reduced; and the effective recovery of the trifluoromethane prevents environmental pollution, and the chloroalkali, the monochlorodifluoromethane and polyvinyl chloride (PVC) can be circularly produced.
Owner:SHANDONG DONGYUE CHEM

Application of supported catalyst in cracking of trifluoromethane

The invention relates to a catalyst used in cracking of trifluoromethane and preparation thereof. The catalyst is characterized by adopting zirconium oxide, magnesium oxide, activated carbon, acid treated activated carbon, alumina and the like as carriers, auxiliaries contain alkali metals K, Na and Cs, carrying capability of active components is 1-50% (mass percent), and molar content of metal auxiliaries is not higher than 50% of the total molar content of the active components and the metal auxiliaries. The catalyst provided by the invention has the characteristics that trifluoromethane catalytic cracking reaction temperature is low and is lower than 600 DEG C, catalyst dosage is low, conversion rate and yield are high, selectivity is high, high temperature resistance and strong acid resistance are good and high value-added products can be obtained; the catalyst is not only effectively improved in thermal stability resistant to high temperature agglomeration but also effectively improved in corrosion resistance through fluorination treatment, so that use stability of the catalyst is improved; and raw materials are available, technology is simple, and industrialization application can be realized.
Owner:SHANGHAI INST OF ORGANIC CHEM CHINESE ACAD OF SCI

Crosslinked polyalcohol membrana body material, method for producing the same and process of using

The invention relates to a main material of a crosslinking polymer film in the technical field of high molecular material and a preparation method and a using method thereof. Through Michael addition polymerization, the invention obtains hyper branched polyamide containing an end double bond. By the protonation of a tertiary amine unit, the introducing of anion ligand and thermal initiation and self crosslinking of the end double bond, the main material of the crosslinking polymer film can be prepared. The components of the material the contents of the weight percentage are as follows: 12 to 19wt percent of amide group, 17 to 29wt percent of methylene, 2 to 3wt percent of protonated tertiary amine and 52 to 66wt percent of fluoroform sulfonate radical. The material of the invention can not only efficiently enrich object dye molecules from an aqueous solution, but also can efficiently enrich precious metal ions from the aqueous solution and restore the metal ions to be internally embedded metal nanoparticles in position. The invention has simple operation and is environment friendly; therefore, the invention can be applied to the treatment of waste water containing dye, the recycling of precious metal or metal-catalyzing and other fields.
Owner:SHANGHAI JIAO TONG UNIV

Catalytic esterification method for sulfonic group functionalization morpholine hyamine ion liquid

The invention discloses a method for catalyzing and esterifying sulfoacid basal functional ion liquid in the formula (1), wherein, n equals to 2, 3 and 4; R is H or C1 to C4 saturated or unsaturated alkyl of straight chain or branched chain; negative ion B- is chlorine, bromine, iodine, sulfate radical, hydrogen sulfate radical, nitric acid radical, dihydrogen phosphate radical, tetrafluoride boric acid radical, hexaflurate phosphoric acid radical, acetic acid radical, methyl sulfoacid radical, paratoluenesulfonic acid radical, fluoroform sulfoacid radical and trifluoroacetic acid radical. The adding dosage of the ion liquid is 0.5 to 100 percent of the total mol of the alcohol and acid, reacting for 0.5 to 12 hours under the normal pressure and the temperature of 20 to 140 DEG C, the esterifying reaction is catalyzed to produce the ester. Compared with the traditional acidic catalyst, the ion liquid simplifies the separation of the product of the esterifying reaction and provides higher selectivity. The invention is distinctly characterized in that the phase separation between the produced ester and the catalyst is automatically finished, and the ion liquid is reusable after simple or non treatment.
Owner:GUANGDONG UNIV OF TECH

Ionic liquid with high electrochemical stability and preparing method thereof

The invention discloses a functional ionic liquid that has high electrochemical stability and a preparation method thereof. Positive ion of the ionic liquid is selected from nitrile-functionalized quaternary ammonium positive ion and negative ion thereof from one of chlorine, bromine, iodine, fluoborate, fluorophosphates, sulfate radical, nitrate radical, trifluoroacetic radical, trifluorochloromethane sulfonic acid group, bi (perfluoroalkyl group sulfonyl) imino negative ion, dinitrile amic radical and saccharin acid radical. Nitrile functional ionic liquid, the negative ion of which is halogen negative ion, is firstly prepared through reaction of pentagons or hexatomic tertiary amine with the alkyl halide that has nitrile functional groups, then ionic liquid that contains different negative ions is prepared by exchange of the negative ions. The ionic liquid has very low melting temperature, can bear the high temperature of 150 DEG C and be stable to water, hardly has vapor pressure but has good electrochemical stability, thereby the invention can be taken as solvent, catalyst ligand, electrochemical electrolyte, etc. that are applied in the fields of organic synthesis, catalytic reaction and lithium-ion battery, etc.
Owner:LANZHOU INST OF CHEM PHYSICS CHINESE ACAD OF SCI

Method for synthesizing crylic acid by catalyzing acetylene carbonyl through palladium

The invention provides a method for synthesizing crylic acid by catalyzing acetylene carbonyl through palladium. Acetylene, carbon monoxide and water are used as raw materials and are catalyzed to synthesize the crylic acid under the conditions that the reaction temperature is between 15 and 70 DEG C and the pressure is between 1.5 and 6MPa. The adopted catalyst uses palladium diacetate as a main catalyst; the dosage of the main catalyst is less than that of a traditional nickel-copper catalyst and is only 1/50; sulfoacid, such as methane sulfonate, trifluoromethane sulfonic acid, p-toluenesulfonic acid or the like, serves as an aid; an addition amount of the additive is that the ratio of n(-SO3H) to n(Pd2<+>) is equal to 1:1-10:1; and organic phosphine such as 2-pyridyl diphenylphosphine (2-PyPPh2) as a ligand. Compared with the nickel-copper catalyst, the catalyst has remarkable advantages that: under the mild conditions, such as the temperature of 40 DEG C and the pressure of 5 MPa, the catalyst can catalyze the acetylene carbonyl to synthesize the crylic acid at high efficiency, can effectively avoid the acetylene and the crylic acid undergoing polymerization and other side reactions, saves energy, and has safe operation and low operating expense.
Owner:CHENGDU ORGANIC CHEM CO LTD CHINESE ACAD OF SCI
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