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43 results about "Nitrosylsulfuric acid" patented technology

Nitrosylsulfuric acid is the chemical compound with the formula NOHSO₄. It is a colourless solid that is used industrially in the production of caprolactam, and was formerly part of the lead chamber process for producing sulfuric acid. The compound is the mixed anhydride of sulfuric acid and nitrous acid.

Synthetic method for 1,2,4-trifluorobenzene

The invention provides a synthetic method for 1,2,4-trifluorobenzene, belongs to the field of pesticide, medicine, and liquid crystal material intermediate preparation, and solves the problem of harshreaction conditions of a current method for synthesizing 1,2,4-trifluorobenzene. The synthetic method for the 1,2,4-trifluorobenzene is characterized by comprising the following steps: performing nitration by using 2,4-dichlorofluorobenzene as a raw material and nitric acid as a nitrating agent to form 2,4-dichloro-5-fluoronitrobenzene in the presence of sulfuric acid; dissolving the 2,4-dichloro-5-fluoronitrobenzene into an organic solvent, adding potassium fluoride and a first catalyst, and performing fluorination under the catalysis of the first catalyst to obtain 2,4,5-trifluoronitrobenzene; dissolving the 2,4,5-trifluoronitrobenzene into a solvent, and performing hydrogenation reduction with hydrogen under the catalysis of a second catalyst to obtain 2,4,5-trifluoroaniline; and performing a reaction on the 2,4,5-trifluoroaniline and sulfuric acid, after a salt is formed, performing a diazotization reaction on the salt and nitroso-sulfuric acid, performing a deamination reductionreaction with sodium hypophosphite under the catalysis of a copper salt, and finally performing steam distillation to obtain the 1,2,4-trifluorobenzene. The method provided by the invention has the advantages of mild reaction conditions and the like
Owner:ZHEJIANG LINJIANG CHEM

Caprolactam production method

The present invention provides a caprolactam production method, which comprises the following processes that: toluene is oxidized under an effect of a cobalt salt catalyst to generate benzoic acid, benzoic acid is subjected to hydrogenation under an effect of a palladium carbon catalyst to generate cyclohexanecarboxylic acid, the cyclohexanecarboxylic acid and nitrosylsulfuric acid are subjected to an amidation reaction in an amidation reactor to generate an amide liquid, cyclohexanone is subjected to an oximation reaction to generate cyclohexanone oxime, the amide liquid and the cyclohexanone oxime are subjected to a rearrangement reaction in a rearrangement reactor, and the reaction product is subjected to processes such as neutralization, crystallization, extraction and refinement to prepare the ??caprolactam, wherein a rearrangement reaction temperature is 70-130 DEG C, pressure is 0-1.0 MPa, and a molar ratio of the acid in the amide liquid to the cyclohexanone oxime is 1-2:1. With the present invention, combination of the two processes such as a toluene method and a cyclohexanone-hydroxylamine method is achieved, a caprolactam yield is increased without increase of ammonium sulfate by-production, nicotinic acid consumption and ammonium sulfate by-production are reduced, the production process is simplified, and construction investment and production cost are saved.
Owner:CHINA PETROLEUM & CHEM CORP

Method for synthesizing 3, 4-dichloro-2-amino-5-fluorobiphenyl

The invention discloses a method for synthesizing 3, 4-dichloro-2-amino-5-fluorobiphenyl. The method comprises the following steps: carrying out diazotization reaction on substrate 3, 4-dichloroaniline and nitroso sulfuric acid to prepare diazonium salt; carrying out a coupling reaction on the diazonium salt and 4-fluoroaniline to obtain the product 3, 4-dichloro-2-amino-5-fluorobiphenyl; sodium chloride needing landfill treatment is not generated in the reaction process, and the method has the characteristics of mild conditions, simple operation, high raw material conversion rate and productselectivity, low energy consumption and the like, and is suitable for industrial production; byproduct sodium sulfate generated by the reaction is a brownish yellow solid; a colorless sodium sulfate product is obtained after resin adsorption decoloration and thermal evaporation concentration crystallization combined process treatment, harmless treatment and resource utilization of sodium sulfate-containing waste salt slag are realized in the whole process, the produced sodium sulfate product reaches the industrial-grade anhydrous sodium sulfate product standard, the economic benefit is improved, and the environmental pollution is avoided.
Owner:ZHEJIANG UNIV OF TECH

Production method and application of nitroso-sulfuric acid

The invention provides a production method of nitroso-sulfuric acid, comprising the following steps: a, heating and dehydrating waste acid produced by diazotization deamination so as to obtain concentrated waste acid, and supplementing concentrated sulfuric acid to prepare mixed acid; b, introducing a gas mixture of exhaust gas produced by a nitrobenzene compound chloro-nitro reaction and the air into a mixed acid spray tower for absorption, detecting nitroso-sulfuric acid prepared in the spray tower and directly pumping qualified nitroso-sulfuric acid into a storage tank of nitroso-sulfuric acid; c, preparing a sodium hydroxide aqueous solution, absorbing tail gas which is not completely absorbed through the spray tower for the preparation of sodium nitrate and sodium chloride; d, adding nitric acid into the tail gas absorption liquid after tail gas absorption until pH of the solution is acidic, regulating pH to neutral level by the use of sodium hydroxide, heating and concentrating the absorption liquid, cooling for crystallization, precipitating out sodium nitrate solid, and continuously carrying out evaporative crystallization to obtain sodium chloride solid. The nitroso-sulfuric acid can be used as a diazotization reagent for the diazotization reaction of weak-base amine containing electron-withdrawing group and heterocyclic amine. The technology has advantages of reasonable design, low energy consumption and simple operation control.
Owner:ZHEJIANG LINJIANG CHEM

Strong-alkali-resistant moderate-temperature disperse violet dye as well as compound mixture and preparation method thereof

ActiveCN106118119AHas the function of strong alkali resistanceBright lusterMonoazo dyesNitrosylsulfuric acidDisperse dye
The invention discloses a strong-alkali-resistant moderate-temperature disperse violet dye as well as a compound mixture and a preparation method thereof. The strong-alkali-resistant moderate-temperature disperse violet dye is a compound of which the structure is as shown in a structural formula (I), and the compound is prepared in the way that 2-bromo-4,6-dinitroaniline or 2-chloro-4,6-dinitroaniline is diazotized by use of nitrosyl sulfuric acid, and the diazotized product is subjected to coupling reaction with m-substituted and o-substituted-N-aniline emulsion. The strong-alkali-resistant moderate-temperature disperse violet dye is environment-friendly in production process, can be applied to moderate-temperature dyeing of such hydrophobic fibers as polyester, nylon and spandex and blended fabrics of the hydrophobic fibers, is bright-colored, can replace disperse violet 28, disperse violet 31 and disperse violet 93, and can be compounded with azo-type disperse dyes and anthraquinone disperse dyes to achieve the functions of adjusting color tone and increasing effect so as to meet the demands of different application conditions. The strong-alkali-resistant moderate-temperature disperse violet dye is high in promotion performance, has favorable fastness in water washing, insolation, sublimation and the like, is excellent in comprehensive performance and has a wide application prospect.
Owner:烟台澳土复合材料有限公司

A kind of production method and application of nitrosyl sulfuric acid

The invention provides a production method of nitroso-sulfuric acid, comprising the following steps: a, heating and dehydrating waste acid produced by diazotization deamination so as to obtain concentrated waste acid, and supplementing concentrated sulfuric acid to prepare mixed acid; b, introducing a gas mixture of exhaust gas produced by a nitrobenzene compound chloro-nitro reaction and the air into a mixed acid spray tower for absorption, detecting nitroso-sulfuric acid prepared in the spray tower and directly pumping qualified nitroso-sulfuric acid into a storage tank of nitroso-sulfuric acid; c, preparing a sodium hydroxide aqueous solution, absorbing tail gas which is not completely absorbed through the spray tower for the preparation of sodium nitrate and sodium chloride; d, adding nitric acid into the tail gas absorption liquid after tail gas absorption until pH of the solution is acidic, regulating pH to neutral level by the use of sodium hydroxide, heating and concentrating the absorption liquid, cooling for crystallization, precipitating out sodium nitrate solid, and continuously carrying out evaporative crystallization to obtain sodium chloride solid. The nitroso-sulfuric acid can be used as a diazotization reagent for the diazotization reaction of weak-base amine containing electron-withdrawing group and heterocyclic amine. The technology has advantages of reasonable design, low energy consumption and simple operation control.
Owner:ZHEJIANG LINJIANG CHEM

Flue gas purification system and method

The invention relates to the field of coal-fired flue gas pollutant purification, and discloses a flue gas purification system and method. The gas purification system comprises a desulphurization tower (10), an oxidation tower (20) and a denitration tower (30) which are communicated in sequence. Oxygen is contained in the oxidation tower. The desulphurization tower is provided with a flue gas inlet used for being communicated with a flue gas delivery pipeline (100), and a first supply device used for supplying a nitrosylsulfuric acid solution into a tower body of the desulphurization tower. The denitration tower is provided with an inlet used for being communicated with an outlet of the oxidation tower, and a second supply device used for supplying a nitric acid solution into a tower body of the denitration tower. According to the gas purification system, as the nitrosylsulfuric acid solution and the nitric acid solution are adopted to remove sulfur dioxide, nitric oxide and mercury, compared with the mode that an FGD process is adopted to carry out desulfurization and then an SCR process is adopted to carry out denitration in the prior art, operating cost is obviously lowered, and equipment investment is small; besides, the occupied area of equipment is small, and the application range is wide.
Owner:CHINA SHENHUA ENERGY CO LTD +3

Fipronil production process

A fipronil production process comprises the following steps that 1, concentrated sulfuric acid and sodium nitrite are used as starting raw materials, reaction is performed in a glacial acetic acid solvent to generate nitrosylsulfuric acid, then a diazo-reaction with arylamine is performed to generate arylamine diazonium salt, then a condensation reaction with dicyan ester is performed, and finally a rearrangement reaction with concentrated ammonia water is performed in an ammonia water medium to generate pyrazol; 2, the pyrazol is dissolved in an acetonitrile solvent, 13 sulfur is rapidly added at the temperature of 20 DEG C for reaction, stirring continues for 30 minutes after the temperature no longer rises, and cooling, filtration and drying are performed to obtain a sulfide product; 3, the sulfide is dissolved in N,N-dimethyl formamide, sodium formate is added and bromotrifluoromethane is introduced under the effect of a catalyst sulfur dioxide for reaction, and a fipronil sulfoxide product is obtained; 4, the fipronil sulfoxide is dissolved in a dichloromethane solvent, an oxidizing agent prepared from sulfuric acid and calcium peroxide is added to perform redox reaction, and alkaline washing, washing, crystallization, centrifugation and drying are performed to obtain a fipronil product. Compared with the prior art, the fipronil production process has the advantages that the process is reasonable and free of risk, the fipronil production process purity is improved, the production efficiency is improved, the production cost is reduced, and the environmental pollution is reduced.
Owner:连云港埃森化学有限公司

Green synthesis method of 3,4,5-trifluorobromobenzene

The invention discloses a green synthesis method of 3,4,5-trifluorobromobenzene. The green synthesis method comprises the following steps: adding 2,3,4-trifluoroaniline and water into a reactor, adding hydrobromic acid and hydrogen peroxide, and carrying out a hybrid reaction to obtain 2,3,4-trifluoro-6-bromoaniline after the reaction is ended; slowly adding a sulfuric acid solution of nitroso sulfuric acid into the prepared 2,3,4-trifluoro-6-bromoaniline, and carrying out a diazotization reaction to obtain a diazonium salt solution; and adding sodium hypophosphite and porous material-loaded copper oxide into the prepared diazonium salt solution as catalysts, conducting reacting, and sequentially carrying out distillation, alkali washing, water washing and reduced-pressure rectification on reaction liquid after the reaction is finished so as to obtain a target product. According to the method, nitrososulfuric acid replaces sodium nitrite to serve as a diazotization reagent, so no high-salt wastewater is discharged, production cost is reduced, and the method is more environmentally friendly; and hydrobromic acid serves as a bromine source, and hydrogen peroxide is added, so the utilization rate of bromine atoms is high, the adding amount of hydrobromic acid is reduced, and the amount of three wastes generated in implementation of the method is remarkably reduced.
Owner:SHANGYU XIES CHEM IND

Production process of 3,5-dichloronitrobenzene

The invention provides a production process of 3,5- dichloronitrobenzene, and belongs to the field of preparation of pesticide intermediates. The method comprises the following steps: adding nitrosylsulfuric acid with the mass fraction of 42% into a reaction kettle, conducting cooling to 5 DEG C, sequentially adding 2,6-dichloro-4-nitroaniline or 4,6-dichloro-o-nitroaniline, isopropanol and desalted water to respectively complete diazotization, denitrification and hydrolysis processes, wherein the temperature of the whole process is not higher than 45 DEG C; conducting steam extraction with water vapor at 100 DEG C to recover isopropanol and acetone, separating diluted sulfuric acid and 3,5-dichloronitrobenzene from a reaction solution after steam extraction, washing 3,5-dichloronitrobenzene with water, carrying out hydrogenation reduction on the washed 3,5-dichloronitrobenzene to produce 3,5-dichloroaniline, carrying out vacuum concentration and high-temperature concentration on thediluted sulfuric acid to obtain 97% concentrated sulfuric acid to prepare nitrosyl sulfuric acid, and separating a sulfuric acid concentrated distillate through an R/O membrane to prepare desalted water, and recycling the desalted water in the process. The process provided by the invention has the advantages of high yield, no pollution and low cost, and is a green production process.
Owner:德兴市德邦化工有限公司

Wet denitration method for high-sulfur flue gas

PendingCN113893671ANo reduction in production qualityPromote reductionGas treatmentNitrogen preparationNitrosylsulfuric acidNitroso
The invention discloses a wet denitration method for high-sulfur flue gas. The method comprises the following steps of 1) purifying, 2) conducting conversion and absorption, (3) discharging gas, and 4) conducting acid production treatment. High-sulfur flue gas self-denitration is carried out by adopting the characteristics that a purified dilute acid aqueous solution absorbs part of nitrogen oxides and concentrated sulfuric acid, and sulfur trioxide reacts with the nitrogen oxides to generate nitroso sulfuric acid. Advanced treatment of nitrososulfuric acid and iron nitrososulfate in the concentrated sulfuric acid is focused, and nitrososulfuric acid and iron nitrososulfate are reduced into nitrogen, water and sulfuric acid or ferrous sulfate through a medicament, so that the final purposes of sulfuric acid wet denitration and no adverse byproducts are achieved, and a complete closed-loop process is formed. According to the denitration system disclosed by the invention, advanced treatment processes such as reduction and purification of nitrososulfuric acid or iron nitrososulfate are also added. Not only are NOHSO4 and Fe(NO)SO4 reduced completely, but also the adverse effect of excess of a small amount of reducing agent is eliminated thoroughly, and the production quality of sulfuric acid is not reduced practically.
Owner:CINF ENG CO LTD

Process for preparing nitroso sulfuric acid by recycling cyclopropylamine to produce tail gas sulfur dioxide

The invention discloses a process for preparing nitroso sulfuric acid by recycling cyclopropylamine to produce tail gas sulfur dioxide. The steps of the process include: S01: obtaining sulfur dioxide gas from a cyclopropylamine production process; S02: sulfur dioxide gas enters a primary absorption kettle and is mixed with The primary absorption liquid in the primary absorption kettle reacts, the tail gas of the primary absorption kettle enters the secondary absorption kettle and reacts with the secondary absorption liquid in the secondary absorption kettle, and the tail gas of the secondary absorption kettle enters the tertiary absorption kettle and reacts with the secondary absorption liquid in the secondary absorption kettle. The tertiary absorption liquid reaction in the tertiary absorption kettle; wherein, the primary absorption liquid and / or the secondary absorption liquid is a mixed acid solution containing sulfuric acid, concentrated nitric acid and nitroso sulfuric acid; the tertiary absorption liquid is sulfuric acid; S03: a The crude product produced by the reaction in the first-stage absorption kettle is transferred to a thin-film evaporator for purification to obtain nitroso-sulfuric acid. It not only realizes the recovery and utilization of tail gas sulfur dioxide, but also separates tail gas absorption and crude product refining through multi-stage absorption kettles and thin film evaporators, which reduces the generation of waste gas in the production process of nitroso sulfuric acid and ensures the quality of nitroso sulfuric acid. .
Owner:江西华飞医药科技有限公司
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