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35results about How to "Overcome the defect of low yield" patented technology

Hydrocarbon catalytic converting method with high butene and light arene yields

ActiveCN106609152AInhibition of hydrogen transfer reactionsFast carbanion cracking reactionTreatment with plural serial stages onlyHydrocarbon oils treatment productsButeneBoiling point
The invention relates to the catalytic cracking field of heavy hydrocarbon class raw materials and particularly discloses a hydrocarbon catalytic converting method with high butene and light arene yields. The method comprises the following steps: 1, enabling a heavy hydrocarbon class raw material to carry out contact reaction with a first cracking catalyst in a first reactor, and then carrying out separation so as to obtain a first carbon depositing catalyst and a first reaction product; 2, enabling light cracked gasoline of which the final boiling point does not exceed 90DEG C to carry out contact reaction with a second cracking catalyst in a second reactor; and 3, directly guiding a reaction mixture which is obtained through reaction in the second reactor into a third reactor without separating the reaction mixture, enabling the reaction mixture to carry out contact reaction with hydrogenation modified cracked light oil of which the boiling range is between 200DEG C and 390DEG C, and then carrying out separation so as to obtain a second carbon depositing catalyst and a second reaction product, wherein the hydrogenation modified cracked light oil is prepared by carrying out hydrogenation treatment on the cracked light oil. High butene yield and high light arene yield can be obtained by the method provided by the invention.
Owner:CHINA PETROLEUM & CHEM CORP +1

Improved method for preparing benzo[d][1,2,3] thiadiazole-7-formic acid trifluoroacetate

The invention relates to a synthesis method of benzo[d][1,2,3] thiadiazole-7-formic acid trifluoroacetate. The synthesis method comprises the following main steps of: performing esterification on m-aminobenzoic acid serving as an initiative raw material and methanol so as to obtain m-aminobenzoic acid methyl ester; in the presence of a surfactant, reacting the m-aminobenzoic acid methyl ester and thiocyanate so as to obtain N-(3-carbomethoxy phenyl)-thiourea; adding bromine into the N-(3-carbomethoxy phenyl)-thiourea in chlorobenzene or glacial acetic acid to perform a cyclization reaction so as to obtain 2-amino-7-carbomethoxy benzothiazole; performing heating and loop opening on the 2-amino-7-carbomethoxy benzothiazole in aqueous solution of KOH and performing diazotization and loop closing under an acid condition so as to obtain 7-carboxylic acid-[1,2,3] diazosulfide; and in the presence of oxalyl chloride, performing an esterification reaction on the 7-carboxylic acid-[1,2,3] diazosulfide and trifluoroethanol so as to obtain a target product. Compared with the prior art, the method increases the yield of the benzo[d][1,2,3] thiadiazole-7-formic acid trifluoroacetate.
Owner:EAST CHINA UNIV OF SCI & TECH

Continuous cyclic preparation method of high-purity lactulose solution and product thereof

The invention belongs to the technical field of oligosaccharide preparation, and relates to a continuous cyclic preparation method of a high-purity lactulose solution and a product thereof. Specifically speaking, the preparation method comprises the following steps: (1) performing lactulose isomerisation; (2) performing acidity adjustment; (3) diluting, dispersing and separating; (4) purifying clear lactulose liquid; (5) performing cyclic utilization of a catalyst. Through the preparation method, high-concentration lactulose solution and a subsequent product thereof can be prepared. Accordingto the continuous cyclic preparation method of the high-purity lactulose solution and the product thereof, sodium metaaluminate/an alkaline matter is taken as an alkaline complexing catalyst for the first time in China, and the conversion rate and lactulose concentration achieved by preparing the lactulose by taking the sodium metaaluminate/an alkaline matter as the alkaline complexing catalyst are far higher than those achieved by adopting a boracic acid/sodium hydroxide system; repeated cyclic use of a sodium metaaluminate catalyst is realized; the defect that precipitate wraps the lactuloseis overcome. The preparation method provided by the invention meets resource-saving and environment-friendly production requirements, and provides beneficial experience and reference for promoting clean, high-efficiency and environment-friendly lactulose industrial production.
Owner:JIANGNAN UNIV

Catalyst and preparation method and application thereof

The invention provides a catalyst and its preparation method and application. The catalyst comprises a carrier and an active component and an auxiliary agent which are loaded on the carrier, wherein the carrier is an activated carbon carrier which has undergone acid pickling and oxidation and has particle size of 200-2000 microns; the active component is the Group VIII metal component; and the auxiliary agent is the Group IVB metal component. When the catalyst provided by the invention is used in preparation of low carbon alcohols from synthesis gas, low carbon alcohols can be prepared at low temperature, and contents of low carbon alcohols, especially methanol and ethanol, in an oil-phase product are high. The preparation method has advantages of mild condition, high conversion per pass and low energy consumption, and is beneficial to industrial popularization.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for increasing yield of major proteins 2 and 3 in royal jelly by liquid chromatography purification

The invention provides a method for increasing yield of major proteins 2 and 3 in royal jelly by liquid chromatography purification. The method comprises steps as follows: royal jelly is dissolved inan extraction buffer solution, the mixture is mixed uniformly and centrifuged, a supernatant is taken, saturated ammonium sulfate is added to the supernatant for precipitation, a supernatant is takenafter centrifugation, filtering is performed by a filter membrane, and a sample buffer solution is obtained; the sample buffer solution is replaced with a buffer solution A with pH being 7.0 by an ultrafiltration centrifuge tube; a royal jelly sample is loaded to a pre-assembled weak cationic chromatographic column balanced by the buffer solution A; the column is subjected to gradient elution by amixed solution of the buffer solution A and a buffer solution B, the ratio of the buffer solution B is gradually increased from 0 to 100%, and major proteins 2 and 3 in the royal jelly are separatedand purified in sequence. According to the method for increasing the yield of the major proteins 2 and 3 in the royal jelly by liquid chromatography purification, abundance of the major proteins 2 and3 in the royal jelly is increased, yield of the major proteins 2 and 3 in the royal jelly is increased, repeatability is good, the yield is high, and the major proteins 2 and 3 in the royal jelly canbe produced on a large scale.
Owner:BEE RES INST CHINESE ACAD OF AGRI SCI

Method for processing inferior diesel oil raw material through moving bed hydrogenation

The invention relates to the field of production of high-value oil products by processing inferior diesel oil, and discloses a method for processing an inferior diesel oil raw material through movingbed hydrogenation. The method comprises: in the presence of hydrogen, introducing an inferior diesel oil raw material into a moving bed hydrorefining reaction unit, and carrying out a first contact reaction with the hydrorefining catalyst contained in the moving bed hydrorefining reaction unit; introducing the hydrogen and the remaining hydrorefining catalyst-separated material into a moving bed hydro-upgrading reaction unit, and carrying out a second contact reaction with the hydro-upgrading catalyst contained in the moving bed hydro-upgrading reaction unit; and separating and fractionating the remaining hydro-upgrading catalyst-separated material to obtain a naphtha product and a product diesel oil. With the method of the present invention, the disadvantages that the use of the fixed bedhydrogenation reactor as the main device can cause the short service life of the catalyst, and the insufficient contact between the oil and gas can cause the low yield of the product oil can be overcome.
Owner:CHINA PETROLEUM & CHEM CORP +1

A method for catalytic conversion of hydrocarbons with high yield of butene and light aromatics

The invention relates to the catalytic cracking field of heavy hydrocarbon class raw materials and particularly discloses a hydrocarbon catalytic converting method with high butene and light arene yields. The method comprises the following steps: 1, enabling a heavy hydrocarbon class raw material to carry out contact reaction with a first cracking catalyst in a first reactor, and then carrying out separation so as to obtain a first carbon depositing catalyst and a first reaction product; 2, enabling light cracked gasoline of which the final boiling point does not exceed 90DEG C to carry out contact reaction with a second cracking catalyst in a second reactor; and 3, directly guiding a reaction mixture which is obtained through reaction in the second reactor into a third reactor without separating the reaction mixture, enabling the reaction mixture to carry out contact reaction with hydrogenation modified cracked light oil of which the boiling range is between 200DEG C and 390DEG C, and then carrying out separation so as to obtain a second carbon depositing catalyst and a second reaction product, wherein the hydrogenation modified cracked light oil is prepared by carrying out hydrogenation treatment on the cracked light oil. High butene yield and high light arene yield can be obtained by the method provided by the invention.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for removing substance difficult to volatilize from wafer

The invention provides a method for removing a substance difficult to volatilize from a wafer, applied to a tungsten etching back process of a deep trench isolation processing process; in the deep trench isolation processing process, the substance difficult to volatilize is generated easily, and the substance difficult to volatilize is attached to the wafer; the method comprises the following steps of S1, putting the wafer into a reaction cavity; S2, heating the wafer, and pumping first reaction gas and second reaction gas to the reaction cavity; S3, controlling the heating temperature on thewafer to remove metal impurities attached on the wafer; and S4, maintaining the flow of the pumped second reaction gas to enable the second reaction gas to be reacted with the substance difficult to volatilize so as to form a volatile substance. The technical scheme has the beneficial effects that the shortcoming of relatively low wafer yield caused by the fact that the substance difficult to volatilize and metal impurities are attached on the wafer in the prior art can be overcome.
Owner:WUHAN XINXIN SEMICON MFG CO LTD

Manufacturing method for unmanned aerial vehicle non-equal-diameter closed square pipe shaped carbon fiber beam

The invention provides a manufacturing method for an unmanned aerial vehicle non-equal-diameter closed square pipe shaped carbon fiber beam so as to effectively solve the technical problems that an existing manufacturing method for the unmanned aerial vehicle non-equal-diameter closed square pipe shaped carbon fiber beam is narrow in application range, demolding is difficult, the airbag core filmyield is low, the service life is short, the flow is complicated, and the cost is relatively high. The manufacturing method for the unmanned aerial vehicle non-equal-diameter closed square pipe shapedcarbon fiber beam comprises the following steps that 1) an upper female die and a lower female die are machined; 2) an upper beam is machined by using the upper female die; 3) a lower beam is machined by using the lower female die; 4) the upper beam and the lower beam are bonded by using a bonding combining tool; and 5) the bonding combining tool is removed to obtain the required non-equal-diameter closed square pipe shaped carbon fiber beam. According to the manufacturing method, an integral component is divided into two parts to be separately formed, compared with integral forming, the requirements on a forming process and a forming tool are relatively low, and the problem of difficult demolding of the non-equal-diameter closed square pipe beam is solved.
Owner:西安爱生无人机技术有限公司
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