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60 results about "P-chlorotoluene" patented technology

Anticorrosive self-cleaning paint

The invention relates to a self-cleaning paint, particularly an anticorrosive self-cleaning paint. The anticorrosive self-cleaning paint is prepared from the following raw materials in parts by weight: 20-30 parts of tetramethyldivinyl disiloxane, 25-40 parts of methylethoxy silicon oil, 10-15 parts of hydroxy hydrogenous silicon oil, 15-20 parts of chlorotoluene, 1-5 parts of ethanedioic acid, 0.1-0.5 part of cyclopentanol and 0.3-0.7 part of catalyst. The anticorrosive self-cleaning paint can not generate shrinkage or release heat, and has the advantages of moderate hardness, favorable thermal conductivity, favorable electric insulativity and high sealability.
Owner:JIANGSU NUOFEI NEW MATERIAL TECH

Cotton topping agent and preparation method thereof

InactiveCN110199997AEffectively control prosperityControl prosperityPlant growth regulatorsBiocidePaichongdingSulfonate
The present invention provides a cotton topping agent, which comprises, by weight, 0.8-2 parts of paichongding, 0.8-2 parts of hydroxypropylmethylcellulose, 3-6 parts of beta-methylnaphthalene, 5-10 parts of fosamine-ammonium, 10-15 parts of isonicotinic acid, 10-15 parts of iodophenoxyacetic acid, 15-20 parts of p-chlorotoluene, and 15-20 parts of sodium disec-octyl maleate sulfonate. According to the present invention, the cotton topping agent is organically dissolved, such that the cotton top can be killed, the cotton length can be effectively controlled, the ideal plant type can be shaped,the flower and the bud can be retained, the photosynthesis of cotton can be enhanced, the cotton boll can be increased, the diseases can be prevented and controlled, the boll opening early maturity can be achieved in advance by more than seven days, the micronaire value of cotton is not affected, and the purposes of high yield and stable production are achieved.
Owner:高俊毅

Production method of p-chlorotoluene

The invention discloses a production method of p-chlorotoluene, comprising the steps of chloridizing toluene, removing toluene and rectifying mixed chlorotoluene. Toluene is chloridized by the steps of placing toluene in a chlorination kettle and adding a catalyst in the chlorination kettle, and feeding chlorine at 40-60 DEG C and carrying out a chlorination reaction. The catalyst used in the chlorination reaction is prepared by the steps of reacting alumina, silicon oxide and sodium oxide react at 120-150 DEG C for 6-8 hours and activating in a high-temperature activation furnace at 800 DEG C for 4-6 hours. The production method provided by the invention is simple and convenient and is easy to operate. In the total content of p-chlorotoluene and o-chlorotoluene in final products, the content of p-chlorotoluene is up to above 80%. After rectification, the content of p-chlorotoluene is up to above 99.5%.
Owner:江苏优普生物化学科技股份有限公司

Mixed chlorotoluene MVR (mechanical vapor recompression) rectification system and method

The invention belongs to the field of chemical industry and relates to a mixed chlorotoluene MVR (mechanical vapor recompression) rectification system and method. The system herein comprises a primarycolumn, an ortho-column, a para-column, evaporators, a cooler, a gas-liquid separation tank, a vapor compressor, reboilers and the like. The system is characterized in that continuous rectification via the primary column, ortho-column and para-column by means of rectification is carried out; mixed chlorotoluene mother liquor that is preheated is processed via the primary column to obtain crude o-chlorotoluene and p-chlorotoluene; the crude o-chlorotoluene and p-chlorotoluene are fed respectively into the ortho-column and the para-column for continued rectification; o-chlorotoluene with purityof higher than 98% is acquired from the top of the ortho-column; p-chlorotoluene with purity of higher than 92% is acquired from the bottom of the ortho-column; distillates from the three columns aresubjected to heat exchanging with liquid water in respective top evaporators; the liquid water absorbs heat and evaporates into water vapor; the water vapor is separated and purified by the gas-liquid separation tank before the resultant is heated and pressurized in the vapor compressor; the pressurized material enters the reboilers at the bottoms of the three columns to release latent heat to heat part of the bottom distillates. The system and method herein have the advantages of high separation efficiency, low energy consumption, low operation cost and the like.
Owner:JIANGSU LEKE ENERGY SAVING TECH CO LTD

Automatic temperature control reaction kettle for synthesizing p-chlorotoluene

The invention discloses an automatic temperature control reaction kettle for synthesizing p-chlorotoluene. The reaction kettle comprises a lower-part stirring paddle, an upper-part stirring paddle, astirring shaft, a water drainage valve, a circulating water valve, a water pump, a controller 1, a heating water tank, an air inlet pipe, an electric valve, a water inlet pipe, a water outlet pipe, afirst water inlet valve, a second water inlet valve, a chlorine gas inlet, a gas distributor, a material inlet pipe, a liquid raw material inlet, a coil water inlet, a gas outlet, a safety valve, a coil water outlet, a motor, a motor reducer, a coil, a liquid outlet, a temperature sensing device, a reaction kettle body, a sealing cover, a sealing ring, a mounting mouth, a jacket, a jacket water inlet, a jacket water outlet, a hot water valve, a cold water valve, a cold water inlet pipe and a controller 2. An automatic temperature control device including the jacket and the coil is adopted by the reaction kettle, so that the problems of too low selectivity caused by excessively high reaction temperature and a too-low conversion rate caused by excessively low reaction temperature are solved,and meanwhile full contact of reactants are achieved through adoption of the two stirring paddles and the gas distributor.
Owner:NINGBO UNIV

Production technology for preparing p-chlorotoluene by methylbenzene directional chlorination

The invention relates to the technical field of chemical raw material preparation, in particular to a production technology for preparing p-chlorotoluene by methylbenzene directional chlorination. Theproduction technology includes the steps: chlorination: adding catalysts into a reaction vessel, adding methylbenzene into the reaction vessel, leading in inert gas, discharging air in the reaction vessel, placing the reaction vessel into a constant temperature device after shading treatment, leading chlorine into a constant temperature device, performing chlorination reaction and chromatographicanalysis and accordingly judging reaction endpoints to obtain chlorinated mixture for standby application; rectification: adjusting reflux ratio to be 10:1 and collecting fraction with the temperature of 158-162 DEG C to obtain o-chlorotoluene and p-chlorotoluene mixed solution for standby application; primary purification; secondary purification. The production technology solves the problems ofpoor methylbenzene chlorination directional selectivity and high cost in the prior art, and is high in p-chlorotoluene yield and conversion rate, good in para-position directional selectivity and reasonable in technological cost.
Owner:JIANGSU QIHENG AGRI & CHEM TECHCO

Special reactor for oriented synthesis of p-chlorotoluene

The invention discloses a special reactor for oriented synthesis of p-chlorotoluene. The special reactor comprises a reactor body 1, wherein a first hollow air inflow board 2 and a hollow liquid inflow board 3 are arranged at the upper part of the reactor body 1; a plurality of nozzles 4 are arranged on the first hollow air inflow board; each nozzle consists of an inner tube, a housing and a spray nozzle; the inner tubes are connected with the first hollow air inflow board 1; the housings are connected with the hollow liquid inflow board 2; a second hollow air inflow board 5 is arranged at the lower part of the reactor body; a plurality of injection orifices are formed in the second hollow air inflow board; the nozzles are arranged opposite to the jetting directions of the injection orifices.
Owner:JIANGSU LIYANG NEW MATERIALS CO LTD

Method for catalyzing chlorination of alkylbenzene ring by using combined catalyst

The invention discloses a method for catalyzing chlorination of alkylbenzene ring by using a combined catalyst. The method comprises the following steps: adding iron powder or Lewis acid which serves as a primary catalyst into a toluene liquid, adding a composition of an elementary substance sulfur and hydroxamic acid, which serves as a cocatalyst, introducing chorine under the condition of keeping out of the sun, controlling the temperature within 0-70DEG C in the whole chlorination process, and controlling the chlorine introducing amount to ensure that the conversion rate of toluene is over 97 percent. After the combined cocatalyst is applied to the chlorination of a benzene ring, the selectivity of a product, namely parachlorotoluene is effectively improved, the selectivity of the parachlorotoluene is over 50 percent and the catalyst is easy to separate.
Owner:SOUTHEAST UNIV

P-benzyldiethoxymethylsilane and preparation method thereof

The invention relates to the field of organic chemistry and provides p-benzyldiethoxymethylsilane and a preparation method thereof. The preparation method solves the problem that in sodium condensation method-based synthesis of p-substituted benzyldiethoxymethylsilane, a large amount of a solvent is used so that environmental pollution is produced and solvent recycle is difficult. The preparation method comprises that the p-benzyldiethoxymethylsilane is synthesized from methyl triethoxysilane and p-chlorotoluene as raw materials by a sodium condensation method. The preparation method does not use a toluene solvent, allows mild reaction conditions, has simple processes and is suitable for large-scale industrial production.
Owner:HANGZHOU NORMAL UNIVERSITY

Preparation method of parachlorobenzoyl chloride

The invention discloses a preparation method of parachlorobenzoyl chloride. The method includes the steps of: (1) chlorination: adding the raw material p-chlorotoluene into a reaction kettle, performing stirring, adding triethanolamine into the reaction kettle, and conducting stirring for 30min, adding thionyl chloride, conducting stirring for 10min, then slowing raising the temperature, adding azodiisobutyronitrile, introducing chlorine gas for reaction to obtain 4-chlorobenzotrichloride; (2) hydrolysis: adding the4-chlorobenzotrichloride obtained in step (1) into a hydrolysis kettle, adding the catalyst ferric trichloride, adding water dropwise to obtain a parachlorobenzoyl chloride crude product; and (3) distillation: distilling the parachlorobenzoyl chloride crude product to obtain the product. Specifically, the p-chlorotoluene is 30000-40000 parts, and triethanolamine is 1-10 parts. P-chlorotoluene is adopted as the raw material for chlorination by chlorine gas to obtain 4-chlorobenzotrichloride, and then hydrolysis and distillation are carried out so as to obtain the product. Firstly triethanolamine is utilized to remove the influence of iron ions, then thionyl chloride is utilized to remove the moisture influence, the chlorination reaction time is short, the reaction by-product is few, and the yield is high.
Owner:山东福尔有限公司
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