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75results about How to "Reduce steric hindrance effect" patented technology

Deep desulfurization hydrotreatment method of diesel oil

The invention discloses a deep desulfurization hydrotreatment method of diesel oil. The method comprises the following steps that a diesel oil raw material enters a hydrogenation reactor and contactsa hydrogenation catalyst bed layer to carry out a hydrogenation reaction, and the reaction product flows out of the reactor, wherein the hydrogenation catalyst bed layer is filled with at least two stages of vulcanization-state hydrogenation catalysts in a grading manner along the material flow direction, the metal active phase crystal lengths of each stage of the vulcanization-state hydrogenationcatalyst are increased stage by stage along the material flow direction, and the lamellar crystal layer number is reduced stage by stage. According to the catalyst grading method disclosed by the invention, the matching reaction of the molecular size and structure of the reactants in each section and an active phase structure can be fully realized so as to effectively utilize the active center ofthe catalyst, improve the coupling reaction performance of the active center structure and the molecular structure, substantially improve the desulfurization activity and the stability of the whole system on reactants, significantly improve the desulfurization depth of diesel oil and produce ultralow-sulfur diesel oil.
Owner:CHINA PETROLEUM & CHEM CORP +1

Double-cross-linking chemical synthesis method of citrinin-protein-coupled antigen and preparation method of anti-citrinin monoclonal antibody

The invention relates to a double-cross-linking chemical synthesis method of a citrinin-protein-coupled antigen and a preparation method of an anti-citrinin monoclonal antibody, belongs to the field of biotechnology. The synthesis method of the citrinin-protein-coupled antigen comprises the following steps that: the citrinin and a double-cross-linking agent (C2H3O)-(CH2)n-(C2H3O) react at first and is then coupled with a carrier, glycine is used for occlusion after reaction, and separation and purification are carried out finally, thereby obtaining the citrinin-carrier-coupled antigen. The preparation method of the anti-citrinin monoclonal antibody comprises the following steps: carrying out cell fusion and screening with the hybridoma technique to obtain a hybridoma cell line of the anti-citrinin monoclonal antibody with stable secretion, preparing ascitic fluid, and purifying, thereby obtaining the anti-citrinin monoclonal antibody. The invention has the advantages of mild preparation conditions, simple operation and controllable process. The obtained anti-citrinin monoclonal antibody has high specificity and high affinity, and can be further used for preparation of the enzyme linked immunosorbent assay kit or test paper card for citrinin detection.
Owner:FUZHOU UNIVERSITY

Heavy oil hydrotreatment method

The invention discloses a heavy oil hydrotreatment method, which comprises the following steps that a heavy oil raw material enters a hydrogenation reactor and contacts a hydrogenation catalyst bed layer to carry out a hydrogenation reaction, and the reaction product flows out of the reactor, wherein the hydrogenation catalyst bed layer is filled with at least two stages of vulcanization-state hydrogenation catalysts in a grading manner along the material flow direction, the average length of the metal active phase crystals of each stage of the vulcanization-state hydrogenation catalyst is increased stage by stage along the material flow direction, the average layer number of the lamellar crystals is reduced stage by stage, the content of the active components is increased stage by stage,and the probable pore diameter is reduced stage by stage. According to the method, the specific catalyst gradation is adopted, so that the active center of the catalyst can be effectively utilized, the coupling reaction performance of an active center structure and a reactant molecular structure is improved, the stability of hydrogenation reaction, such as demetalization, desulfurization, denitrification and the like, of the whole system is greatly improved, and deep hydrogenation of heavy oil is facilitated.
Owner:CHINA PETROLEUM & CHEM CORP +1

Grading method of fluidized bed catalyst

The invention discloses a fluidized bed catalyst grading method which comprises the following steps: heavy oil raw materials and hydrogen enter from the bottom of a reactor and are in contact with a hydrogenation catalyst bed layer for hydrogenation reaction, and a reaction product flows out from the top of the reactor; wherein the grading is filled with at least two stages of sulfurized hydrogenation catalysts; wherein from bottom to top in the material flow direction of the sulfurized hydrogenation catalysts at each stage, the average length of metal active phase crystals is gradually increased, the average number of lamellar crystal layers is gradually reduced, the content of active components is gradually reduced, the probable pore diameter is gradually reduced, the stacking density isgradually reduced, and the particle diameter is gradually reduced. The metal active phase is active metal sulfide. According to the method, the specific catalyst gradation is adopted, so that the active center of the catalyst can be effectively utilized, the coupling reaction performance of an active center structure and a reactant molecular structure is improved, the stability of hydrogenation reaction, such as demetalization, desulfurization and denitrification, of the whole system is greatly improved, and deep hydrogenation of heavy oil is facilitated.
Owner:CHINA PETROLEUM & CHEM CORP +1

Synthesis method of tert-butyl acetoacetate

The invention discloses a synthesis method of tert-butyl acetoacetate. The method comprises the following steps that tertiary butanol and catalysts are added into a reaction container; the catalysts are selected from aliphatic amine catalysts or tertiary amine catalysts; or the catalysts are fatty amine catalysts and tertiary amine catalysts; the catalysts are one kind of catalysts or several kinds of catalysts proportioned at any proportion; the temperature is raised to 20 to 120 DEG C; diketene is dropwise added; in the reaction process, the reaction temperature is controlled to be 20 to 150DEG C; after the dripping is completed, the temperature is controlled at 20 to 150 DEG C; heat insulation is performed for 0.5 to 8 hours to obtain tert-butyl acetoacetate raw ester; the mole ratio of the tertiary butanol to the diketene is (1 to 2) to1; the addition of the catalyst is 0.1 weight percent to 2 weight percent of the total amount. The process is used for synthesizing the tert-butylacetoacetate; the conversion rate of the diketene reaches 100 percent; the finished product yield reaches 94 percent or higher; the product content reaches 99 percent or higher. By using the process,the synthesis yield is greatly improved; the preparation cost is reduced; meanwhile, the three-waste quantity is reduced; no corrosion is caused on the equipment; better economic and environment-friendly effects can be achieved.
Owner:NANTONG ACETIC ACID CHEM
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