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48 results about "Nitrochlor" patented technology

Preparation method of paranitroaniline

The invention relates to a preparation method of paranitroaniline. The preparation method comprises the following steps that: (1) a high-pressure conveying pump is used for respectively pumping p-nitrochlorobenzene and stronger ammonia water with the concentration being 45 to 55 weight percent into a tubular mixer according to a weight ratio of 1:(3.0-4.0), and a mixed material is obtained through sufficient mixing; (2) the mixed material is continuously conveyed into a pipeline reactor for reaction, the reaction temperature is 235 DEG C to 245 DEG C, the pressure is 10.0 to 14.0MPa, the reaction time is 40 to 90 minutes, after the reaction is completed, the materials are discharged into a low-pressure reaction kettle by a pressure relief valve, and ammonia is recovered through ammonia release; and (3) after the ammonia recovery, the separation is carried out, the materials are centrifuged and washed after the separation completion, and the paranitroaniline is obtained after the materials are centrifuged to the dry state. The method provided by the invention belongs to a method for continuously producing the paranitroaniline, the production is safer, the production capability is higher, the appearance and the purity of the obtained products are respectively improved, the product quality is excellent, and in addition, the cost is reduced.
Owner:苏州市罗森助剂有限公司

O-chloroaniline preparation method

The invention provides ano-chloroaniline preparation method, wherein the raw materials comprise: o-nitrochlorobenzene, a catalyst, dicyandiamide, a solvent, nitrogen and hydrogen. According to the invention, Ru/C is used as the catalyst, and has characteristics of simple components, stable activity and high selectivity, and dicyandiamide is used as the dechlorination inhibitor, so that the dechlorination side reaction is effectively inhibited, the conversion rate is high, and the selectivity is high; by improving the structure of the rectifying tower, the vapor-liquid mass transfer performancein heat transfer and mass transfer is improved, and the contact area between the gas phase and the liquid phases is increased by utilizing the auxiliary member; the turbulent flow degree is effectively increased through the inflow weir having the step structure and the turbulent flowblock, so that the mass transfer and heat exchange efficiency and the mass transfer and heat exchangerate between the gas phase and the liquid phases are improved; and the treatment and circulation capacities of the liquid phase are improved through the circulation tank, and the gas-liquid phase contact time is favorably prolonged by using the baffle arrangement of the downcomer and the inner diameter change, so that the yield and the purity of o-chloroaniline are improved.
Owner:滨海县星光化工有限公司

Preparation method of chloroprocaine hydrochloride

The invention belongs to the technical field of organic drug synthesis and particularly relates to a preparation method of chloroprocaine. The preparation method includes the steps that 1, 2-chloro-4-nitrobenzoic acid and 2-diethylaminoethanol reaction raw materials are added into a xylene reaction solvent, para-toluenesulfonic acid or immobilized liquid acid or faintly acid metal salt is added to serve as a catalyst, heating is conducted till reflux is achieved, a reaction is carried out for a certain period of time, aftertreatment is carried out, and a water solution of nitrochlor cain is obtained; 2, ammonium chloride and iron powder are added into the water solution of nitrochlor cain, a heating reaction is carried out, aftertreatment is carried out, and crude chloroprocaine hydrochloride is obtained; refining is carried out, and chloroprocaine hydrochloride is obtained. The direct esterification reaction time is short, the production period is shortened by 30% or above, the total yield of the finished product is larger than 30%, and energy consumption is reduced by 25% or above. The content of chloroprocaine hydrochloride is not smaller than 99.0%, the content of related substances is not larger than 1.0%, and the content of a residual solvent (dimethylbenzene) does not exceed 0.1%. The preparation method is suitable for industrial production.
Owner:WUXI KAIFU PHARMA

2-arylmethylthio-6-(tetrahydroquinoline-1-methyl)-4-pyrimidinone derivatives and their preparation methods and applications

The present invention provides a 2-[(substituted phenylamino)carbonylmethylthio]-6-(2,6-dichlorobenzyl)-3H-pyrimidin-4-one derivative, the general structural formula I is as follows: Where R1 is: H, methyl or ethyl; R2 is: 2-bromoacetophenone, p-methyl-2-chloroacetophenone, p-chloro-2-chloroacetophenone, p-nitro- 2-chloroacetophenone, p-cyano-2-chloroacetophenone, p-methoxy-2-chloroacetophenone, p-fluoro-2-chloroacetophenone, benzyl bromide, p-methyl Benzyl chloride, p-chlorobenzyl chloride, p-nitrobenzyl chloride, p-cyanobenzyl chloride, p-methoxybenzyl chloride or p-fluorobenzyl chloride. The invention also relates to a preparation method of the compound and its application as an HIV inhibitor.
Owner:SHANDONG UNIV

Clean production method of 2, 4-dinitrochlorobenzene

The invention provides a clean production method of 2, 4-dinitrochlorobenzene, which comprises the following steps: by taking o-nitrochlorobenzene with the mass fraction of 99% as a raw material and a mixed acid solution prepared from sulfuric acid and nitric acid with the mass fraction of 98% as a nitrating agent, carrying out a continuous nitration reaction in a tubular reactor, pumping the nitrated mixed solution into a heat preservation kettle, after keeping the temperature for 2 hours, pumping the nitration mixed solution into a liquid separation kettle, and separating an upper-layer oil phase, namely a mixed solution of 2, 4-dinitrochlorobenzene and 2, 6-dinitrochlorobenzene, and a lower-layer water phase, namely a waste acid solution; adding fuming sulfuric acid into the separated waste acid solution, so that the moisture content in the waste acid solution is 2% or below; neutralizing the separated mixed solution of 2, 4-dinitrochlorobenzene and 2, 6-dinitrochlorobenzene, washing with water and performing crystallization separation, and obtaining the main product 2, 4-dinitrochlorobenzene and the by-product 2, 6-dinitrochlorobenzene. The continuous production process is adopted, the cost is reduced, prepared waste acid is mechanically applied, waste acid emission is reduced, and the environmental burden is relieved.
Owner:天津泰研科技发展有限公司

Method for preparing DCB reduzate through continuous catalytic hydrogenation reduction

The invention provides a method for preparing a DCB reduzate through continuous catalytic hydrogenation reduction. The method comprises the following steps: adding o-nitrochlorobenzene, toluene, caustic soda liquid with a concentration of 30%, desalted water and a Pt/C catalyst into three continuous tank reactors connected in series, and ending a first-stage intermittent reaction until all reactions do not absorb hydrogen; opening overflow discharge valves of the three tank reactors, and simultaneously pumping o-nitrochlorobenzene, methylbenzene, caustic soda liquid with the concentration of 30% and desalted water into the first tank reactor in proportion by using a metering pump; and continuously introducing hydrogen for catalytic hydrogenation to prepare the DCB reduzat, namely, 2,2-dichlorohydrazobenzene. According to the invention, the loss of the catalyst due to frequent filtering in a batch reaction process can be effectively reduced, internal recycling of the catalyst is achieved, and the service life of the catalyst is prolonged; meanwhile, the tank reactors are relatively small in size, reaction stability is good, product dechlorination is relatively low, selectivity is high and relatively few byproducts is produced; and in addition, exhaust emission in the continuous reaction is greatly reduced, so the environmental pollution is greatly reduced.
Owner:ZHEJIANG QINYAN TECH CO LTD
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