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60 results about "Sulfur monochloride" patented technology

Disulfur dichloride is the chemical compound of sulfur and chlorine with the formula S 2 Cl 2. Some alternative names for this compound are sulfur monochloride (the name implied by its empirical formula, SCl), disulphur dichloride (British English Spelling) and sulphur monochloride (British English Spelling).

Continuous-pressure-changing rectification method and device for preparing medicine-level sulfoxide chloride

The invention relates to a continuous-pressure-changing rectification method and a device for preparing medicine-level sulfoxide chloride. With the adoption of the pressure-changing rectification method, an indirect sequence of carrying out heavy component removal and then carrying out light component removal is adopted as a rectification sequence, so that the decomposition of sulfoxide chloride at high temperature is reduced; sulfur is coarsely mixed with raw materials, sulfur is mixed with tower top gas of a heavy component removal tower, and a low-boiling-point substance, namely sulfur dichloride which is hard to remove, is fundamentally converted into a high-boiling-point substance, namely sulfur monochloride which is easy to remove, due to multistep sulfur adding; and a catalyst is added, so that the dissolution rate and reaction rate of the sulfur are accelerated. The heavy component removal tower is subjected to normal-pressure operation; and a light component removal tower is subjected to depressurized operation. The energy consumption of operation is reduced, and the decomposition reaction of the sulfoxide chloride hardly carries out under depressurized conditions, so that the probability that the color and luster of products are polluted by sulfur dichloride is greatly reduced, high-purity and colorless sulfoxide chloride products are produced from tower bottoms, and the content is over 99.9%.
Owner:TIANJIN UNIV

Method for rectifying thionyl chloride

The invention discloses a method for rectifying thionyl chloride. A two-stage continuous rectification process is adopted. The method comprises the following steps of: continuously feeding a crude product of the thionyl chloride into a first-stage rectification column, continuously extracting sulfur monochloride from a column bottom of the first-stage rectification column, and continuously extracting a semifinished product of the thionyl chloride from a lateral line; and continuously feeding the semifinished product of the thionyl chloride into a second-stage rectification column, continuously extracting a finished product of the thionyl chloride on a column top of the second-stage rectification column, and feeding a mixture on a column bottom into the first-stage rectification column. Overcuring devices are arranged between the first-stage rectification column and a condenser connected therewith and between the second-stage rectification column and a condenser connected therewith. The rectification method can realize continuous large-scale production, can maintain the relatively stable yield and quality of products and has high energy utilization rate, high degree of automation and easy control of operation. Compared with the conventional discontinuous rectification, the method for rectifying the thionyl chloride has the advantages of remarkable improvement of the production capability of a single device, large-scale production, guarantee of production safety, reduction of production cost, and good economic benefit.
Owner:CHINA PINGMEI SHENMA GRP KAIFENG DONGDA CHEM

Green synthesis technology of O,O-diethyl thiophosphoryl chloride

The invention provides a green synthesis technology of O,O-diethyl thiophosphoryl chloride and relates to the field of chemical synthesis. The green synthesis technology comprises the following steps:taking O,O-diethyl dithiophosphate to react with chlorine gas at low temperature, so as to obtain a crude product of the O,O-diethyl thiophosphoryl chloride; then transferring the crude product to react at high temperature; enabling the residual O,O-diethyl dithiophosphate to further completely react with the chlorine gas. Meanwhile, in a high-temperature reaction process, a polymeric compound isprevented from being generated when a compound catalyst is used and sulfur monochloride impurities are completely removed through reaction, so that a byproduct sulfur has a crystalline state and a product more easily separated and purified. Moreover, HCl and sulfur-containing odorous gas are pumped away through applying negative pressure and the tail gas is absorbed to prevent air pollution. In awhole reaction process, technological water does not need to be added, so that wastewater is not generated and the treatment cost of sulfur-containing and phosphorus-containing wastewater is reduced.The technology has the advantages of simplicity in operation, easiness for obtaining raw materials, moderate reaction conditions, small pollution and environment friendliness.
Owner:CHONGQING HUAGE BIOCHEM

Reclaimed rubber activator sulfo synthetic method

The present invention provides a reclaimed rubber activator sulfo synthetic method, and relates to reclaimed rubber additive production technical field, the reclaimed rubber activator sulfo synthetic method comprises the following steps: antioxidant mother liquor is melted, the melted antioxidant mother liquor is pumped into a reactor, each reactor is fed with 2.8 tons of the material; the antioxidant mother liquor is heated to 120 DEG C, and stirred and dewatered for 40 minutes, and the temperature is dropped to 80 DEG C; under stirring conditions, a certain quantity of sulfur monochloride is dropwise added, the temperature gradually rises to 140 to 145 DEG C for high temperature synthesis; after the material is fed, the material is stirred for 30 minutes, the reactor is heated to 120 DEG C, after 2 hours of thermal insulation, the reactor is heated to 140 DEG C, after 2 hours of thermal insulation, the material in the reactor is transferred into a finished product packaging kettle, and stirred and cooled to 85 DEG C, and the material is packed to obtain a finished product. The reclaimed rubber activator sulfo synthetic method has the advantages of simple process and easy control of the process conditions, and the synthesized reclaimed rubber activator has the characteristics of no smell, less dosage and good effect, and compared with the activator synthesized by a conventional method, the dosage can be reduced by more than 50%.
Owner:安徽金马橡胶助剂有限公司

Preparation method for sulfur-containing carbofuran derivative with less than 0.1% of harmful impurity carbofuran

ActiveCN102786503ATroubleshoot incomplete responsesSolve the technical problem of high carbofuran contentOrganic chemistryCarbofuranEthane Dichloride
The invention discloses a preparation method for sulfur-containing carbofuran derivative with less than 0.1% of harmful impurity carbofuran. The preparation method comprises the following steps of: using di-n-butylamine or N-isopropyl-beta-alanine ethyl ester derivative and sulfur monochloride as raw materials to prepare into disulphide in the presence of an acid-binding agent triethylamine and an organic solvent 1, 2-dichloroethane; and then reacting with a chlorinating agent sulfuryl chloride to obtain nitrogen sulfur chlorine; and finally reacting with carbofuran under the effect of a cosolvent N-methyl-2-pyrrolidone or dimethylformamide so as to obtain the sulfur-containing carbofuran derivative with not less than 96% of quality percentage composition and less than 0.1% of main harmful impurity carbofuran. By adopting the preparation method, the problem that the carbofuran cannot be completely reacted during being reacted can be solved, the defects due to low content and low yield of sulfur-containing carbofuran derivatives such as benfuracarb and carbosulfan caused by a solid-liquid two-phase reaction can be avoided, the technical problem due to relatively high content of main harmful impurity carbofuran can be solved, and the content of the sulfur-containing carbofuran derivatives such as benfuracarb and carbosulfan can reach a value not less than 96%, and the yield is 97 to 98%, and the main harmful carbofuran in the product is less than or equal to 0.1%, so that the preparation method has a wide popularization and application prospect.
Owner:湖南海利常德农药化工有限公司

Preparation method for sulfur-containing carbofuran derivative with less than 0.1% of harmful impurity carbofuran

ActiveCN102786503BTroubleshoot incomplete responsesSolve the technical problem of high carbofuran contentOrganic chemistryCarbofuranEthane Dichloride
The invention discloses a preparation method for sulfur-containing carbofuran derivative with less than 0.1% of harmful impurity carbofuran. The preparation method comprises the following steps of: using di-n-butylamine or N-isopropyl-beta-alanine ethyl ester derivative and sulfur monochloride as raw materials to prepare into disulphide in the presence of an acid-binding agent triethylamine and an organic solvent 1, 2-dichloroethane; and then reacting with a chlorinating agent sulfuryl chloride to obtain nitrogen sulfur chlorine; and finally reacting with carbofuran under the effect of a cosolvent N-methyl-2-pyrrolidone or dimethylformamide so as to obtain the sulfur-containing carbofuran derivative with not less than 96% of quality percentage composition and less than 0.1% of main harmful impurity carbofuran. By adopting the preparation method, the problem that the carbofuran cannot be completely reacted during being reacted can be solved, the defects due to low content and low yield of sulfur-containing carbofuran derivatives such as benfuracarb and carbosulfan caused by a solid-liquid two-phase reaction can be avoided, the technical problem due to relatively high content of main harmful impurity carbofuran can be solved, and the content of the sulfur-containing carbofuran derivatives such as benfuracarb and carbosulfan can reach a value not less than 96%, and the yield is 97 to 98%, and the main harmful carbofuran in the product is less than or equal to 0.1%, so that the preparation method has a wide popularization and application prospect.
Owner:湖南海利常德农药化工有限公司

Continuous-pressure-changing rectification method and device for preparing medicine-level sulfoxide chloride

The invention relates to a continuous-pressure-changing rectification method and a device for preparing medicine-level sulfoxide chloride. With the adoption of the pressure-changing rectification method, an indirect sequence of carrying out heavy component removal and then carrying out light component removal is adopted as a rectification sequence, so that the decomposition of sulfoxide chloride at high temperature is reduced; sulfur is coarsely mixed with raw materials, sulfur is mixed with tower top gas of a heavy component removal tower, and a low-boiling-point substance, namely sulfur dichloride which is hard to remove, is fundamentally converted into a high-boiling-point substance, namely sulfur monochloride which is easy to remove, due to multistep sulfur adding; and a catalyst is added, so that the dissolution rate and reaction rate of the sulfur are accelerated. The heavy component removal tower is subjected to normal-pressure operation; and a light component removal tower is subjected to depressurized operation. The energy consumption of operation is reduced, and the decomposition reaction of the sulfoxide chloride hardly carries out under depressurized conditions, so that the probability that the color and luster of products are polluted by sulfur dichloride is greatly reduced, high-purity and colorless sulfoxide chloride products are produced from tower bottoms, and the content is over 99.9%.
Owner:TIANJIN UNIV

Synthesizing method for fipronil intermediates

The invention relates to a synthesizing method for fipronil intermediates. The synthesizing method for the fipronil intermediates effectively solves problems of low production yield in preparation of the fipronil intermediates, complicated operation, low purity and difficulty in industrialized production. The method includes steps of adding 5-amino-3-cyano-1-(2, 6-dichloro-4-trifluoromethyl phenyl) pyrazole into a polar solvent at first and blending the 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethyl phenyl) pyrazole evenly, heating the 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethyl phenyl) pyrazole to 30-70 DEG C under 0.3-0.6 atmosphere, distilling one sixth of the polar solvent, and then cooling the 5-amino-3-cyano-1-(2, 6-dichloro-4-trifluoromethyl phenyl) pyrazole to 20 DEG C, quickly adding sulfur monochloride to react for half an hour under the conditions of 35-40 DEG C and negative pressure of -0.095--0.01MPa, obtaining a mixture which is standing for half an hour under the conditions of 35-50 DEG C and one atmosphere so as to remove hydrogen chloride, adding an amine regulator to regulate a PH value as 7, cooling the mixture to </=5 DEG C, filtering to obtain a filtered object which is washed by water, and drying to obtain 5-amino-1-(2,6-dichloro-4-trifluoromethyl phenyl)-3-cyano pyrazole-4-base double sulfur. The synthesizing method for the fipronil intermediates is prepared by simple process and operated under mild reaction conditions, high in production yield and purity, low in production cost, easy to produce in an industrialized manner and capable of serving as the intermediate to effectively prepare fipronil.
Owner:HENAN UNIV OF CHINESE MEDICINE

Synthetic process for sulfurized calcium alkyl phenolate clearing agent

InactiveCN106367160ASolve the unsafe problem of high temperature spontaneous combustionMeet industry requirementsAdditivesSpontaneous combustionHydrogen sulfide poisoning
The invention provides a synthetic process for a sulfurized calcium alkyl phenolate clearing agent. The synthetic process comprises the following steps: adding dodecylphenol into a three-neck bottle with a stirring function, mounting a condenser tube and an absorption bottle and adding sulfur monochloride into the three-neck bottle for sulfuration so as to obtain sulfurized alkyl phenate; pouring sulfurized alkyl phenate into a neutralization kettle, adding base oil and an aqueous solution of calcium chloride and adding calcium oxide for a neutralization reaction; after completion of neutralization, adding the solvent glycol, stearic acid and calcium oxide, introducing CO2 and carrying out carbonation once; after completion of carbonation, adding calcium oxide into the neutralization kettle, introducing CO2 and continuing carbonation twice to three times; and carrying out pressure-reduced distillation and filtering so as to obtain the product sulfurized calcium alkyl phenolate. The synthetic process has the advantages that the process is simple and rational, can prevent the unsafe factor of spontaneous combustion of sulfur dust at high temperature and the accident of hydrogen sulfide poisoning caused by leakage of hydrogen sulfide, overcomes the problem of emission of exhaust gas and waste water in the process of sulfuration of alkylphenol, and enables by-products to be recycled.
Owner:朝阳中联化工有限公司
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