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82results about How to "Lower reaction yield" patented technology

Simulated moving bed reaction and regeneration device for solid acid alkylation and raw material reaction and catalyst regeneration method

The invention discloses a simulated moving bed reaction and regeneration device for solid acid alkylation and a raw material reaction and catalyst regeneration method. The device comprises a raw material and product zone, a regeneration material zone, a rotary valve and a counter-current simulated moving bed reactor. Under control of the rotary valve, a raw material in the raw material and product zone is introduced into the counter-current simulated moving bed reactor for an alkylation reaction, a product produced in the counter-current simulated moving bed reactor returns to the raw material and product zone, a catalyst regeneration medium in the regeneration material zone is introduced into the counter-current simulated moving bed reactor for catalyst regeneration, and a material produced after catalyst regeneration in the counter-current simulated moving bed reactor returns to the material regeneration zone. By means of the device and the method, the continuous and stable operation of the solid acid alkylation reaction, product extraction, moderate catalyst generation and deep catalyst generation is achieved, the operation cycle and the service life of the device are prolonged, and the operation economy of the device is greatly improved.
Owner:CHINA PETROLEUM & CHEM CORP +1

Catalyst for preparing acrylonitrile by ammonia oxidizing method

The present invention relates to a fluidized bed catalyst for producing acrylonitrile by using ammonia oxidation process. It is characterized by that said catalyst uses silicone dioxide or aluminum oxide or their mixture as carrier, and contains the following active components: Mo, Bi, Fe, Ni, X, Y, Z and Q, in which X is at least one kind selected from Mg, Co, Ca, Be, Cu, Zn, Pb, Mn or Te, Y is at least one kind selected from La, Ce or Sm, Z is at least one kidn selected from K, Rb, Na, Li o Cs and Q is at least one kidn selected from Ti, Zr, Nb or Sb. Said catalyst can be used in industrial production of acrylonitrile by using propene ammonia oxidation process.
Owner:CHINA PETROLEUM & CHEM CORP +1

Furfural preparation process

The invention discloses a furfural preparation process. The furfural preparation method adopts a two-step method. The method comprises the following specific steps: firstly, catalyzing hydrolysis of hemicellulose in corncobs by adopting an SO4 < 2-> / Fe2O3-alpha-Al2O3 supported solid acid catalyst; then catalyzing corncob hydrolysis reaction liquid to prepare furfural by using a novel catalyst instead of sulfuric acid, stripping crude aldehyde in the reaction system by using nitrogen instead of water vapor, performing alkali washing and refining on the stripped crude aldehyde by using a continuous centrifugal extraction refining method, introducing the crude aldehyde into a rectifying tower, and rectifying to obtain furfural with the purity of over 99%. According to the method, the furfuralis prepared through the two-step method, lignin and cellulose in the corncob residues can be reserved for reuse, the concentration of the crude aldehyde is increased through nitrogen steam stripping,the furfural production yield is increased, and the wastewater yield is reduced.
Owner:QINGDAO UNIV OF SCI & TECH

Preparation device and preparation method of nicarbazin

The invention provides a preparation method of nicarbazin. The preparation method includes the following steps: 1, adding wet paranitroaniline and a solvent into a reaction bottle, and conducting heating, refluxing and water separation; 2, after conducting water distribution, conducting cooling to the room temperature, adding bis(trichloromethyl)carbonate, then conducting heating and stirring to obtain 4, 4'-binitro diphenylcarbamide, and absorbing the generated hydrogen chloride gas with the solvent; 3, adding the liquid absorbing the hydrogen chloride gas as a reaction solvent in another reaction bottle, and adding acetylacetone and urea for a reaction to generate 2-hydroxyl-4,6-dimethyl pyrimidine hydrochloride; 4, regulating the obtained 2-hydroxyl-4,6-dimethyl pyrimidine hydrochloride to be alkaline, then allowing 2-hydroxyl-4,6-dimethyl pyridine hydrochloride to react with 4,4'-binitro diphenylcarbamide in a solution to generate the nicarbazin under the stirring condition, and conducting processing to obtain the finished product of the nicarbazin. The special devices are used and comprise a reaction kettle, a condenser, a gas-liquid separator, a water separator, an anti-inverse-suction one-way valve, an absorption kettle and a second reaction kettle. The raw materials are fully utilized, the product yield is high, the cost is low, and the three wastes are few.
Owner:HUBEI ZHONGMU ANDA PHARMACEUTICAL CO LTD +1

Tetrabutyl tin preparation method

The invention discloses a tetrabutyl tin preparation method. The preparation method comprises the following steps: adding magnesium powder and an ether solvent into a reactor with a stirring and refluxing device, starting to stir and heat till refluxing; then adding a small quantity of chlorobutane and a YF-017 catalyst, slowly adding a mixed solution of chlorobutane and anhydrous tin tetrachloride dropwise, conducting a refluxing reaction to the end after finishing adding; cooling to the normal temperature, adding hydrochloric acid while stirring, then allowing standing still for layering; releasing an aqueous phase on the lower layer, distilling an organic phase at the normal pressure, changing to perform reduced pressure distillation after the solvent is completely distilled, and collecting a fraction of 148-150 DEG C under the condition of the vacuum degree of minus 650 Pa, to obtain tetrabutyl tin. A small quantity of catalyst is added into a one-step reaction device, the Grignardreaction is started immediately, the heat produced in the Grignard reaction in the first step is rapidly absorbed by the alkylation reaction in the second step. Therefore, the phenomenon of materialspraying of the reaction is avoided, and safety in the industrial production is guaranteed.
Owner:SHANGHAI NO 4 REAGENT & H V CHEM

Preparation method of ticagrelor key intermediate aromatic cyclopropanamide

The invention discloses a preparation method of a ticagrelor key intermediate, aromatic cyclopropanamide. The method comprises the following steps: with (1R,2R)-2-(3,4-difluorophenyl)-1-cyclopropyl formate (I) as an initial raw material, carrying out transesterification with formamide under the action of alkali, and meanwhile, maintaining negative pressure or normal pressure to generate a target product, namely, (1R,2R)-2-(3,4-difluorophenyl)-1-cyclopropyl formamide (II). According to the invention, the three-step synthesis reaction in the prior art is simplified by a one-step reaction, and amide is directly generated by formate reaction; therefore, according to the method, reaction steps are saved, the reaction period is shortened, reaction conditions are milder, high-temperature and high-pressure reaction conditions are avoided, and potential safety hazards are greatly reduced. Meanwhile, the raw materials and reagents of the method are low in price, easy to purchase and high in reaction yield, so that the method is low in reaction cost, and industrial production is easy to achieve.
Owner:KAIYUAN HENGTAI PHARMA

Method of synthesizing arbutin by using solid superacid as catalyst

A dehydrant for a dehydration reaction of a key intermediate for synthesizing arbutin in the existing technical route is boron trifluoride diethyl etherate; ether belongs to a flammable and explosivearticle; another dehydrant is strong acid such as sulfuric acid and p-toluenesulfonic acid; such dehydrant is poor in reaction selectivity and very low in yield, generates much waste acid at the sametime and causes very high environmental protection pressure. For that reason, the invention provides a method of synthesizing arbutin by taking solid superacid as a catalyst. The method comprises thefollowing steps: preparing a solid superacid catalyst, preparing an intermediate Arb-1 by using the solid superacid as the catalyst, preparing an intermediate Arb-2 from Arb-1 by using the solid superacid as the catalyst, recovering and activating the catalyst, and performing reaction and purification using the intermediate Arb-2, methanol and sodium methoxide to form arbutin. The method has the advantages that the method causes little waste gas, waste water and industrial residue, and is green, environmentally friendly, simple and convenient in technical operation and suitable for industrialization.
Owner:和德化学(苏州)有限公司

Synthetic method of bis(2,2,2-trinitro ethyl)-3-6-diamino tetrazine

The invention discloses a synthetic method of bis(2,2,2-trinitro ethyl)-3-6-diamino tetrazine of the following formula. The method is characterized by using 3,6-diamino tetrazine and trinitro ethanol as raw materials, adding dimethyl sulfoxide of 3,6-diamino tetrazine in an aqueous solution of trinitro ethanol at low temperature under acidic conditions, and reacting at room temperature to obtain bis(2,2,2-trinitro ethyl)-3-6-diamino tetrazine. The invention is mainly used for synthesizing bis(2,2,2-trinitro ethyl)-3-6-diamino tetrazine.
Owner:XIAN MODERN CHEM RES INST

Method for continuously maintaining performance of catalyst for cyclohexene production

The invention discloses a method for continuously maintaining the performance of a catalyst for cyclohexene production. The method comprises steps: firstly, the feeding amount of a reactor is reduced,a certain amount of a low-activity catalyst is discharged, meanwhile, a corresponding amount of zinc sulfate is added to maintain the concentration of a slurry in the hydrogenation reactor, then a proper amount of a new catalyst is added in batches, the overall activity of the catalyst in the reactor is adjusted, wherein the low-activity catalyst is an old catalyst which operates in the reactor for a long time which is close to the service life. According to the method, two years are taken as a replacement period, the catalyst in the reactor is quantitatively replaced, and the total replacement amount is 30-60Wt% of the total amount of the catalyst in the reactor. According to the method disclosed by the invention, the unit consumption of the new catalyst is reduced, the catalyst adjusting time is shortened, the cost is effectively reduced, and the continuity of a production system is maintained.
Owner:HENAN SHENMA NYLON CHEM
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