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1553results about How to "Improve technical effect" patented technology

High-strength multifunctional pressure-bearing pot cover

InactiveCN106859298AOvercoming indecent structuresReduce thermal efficiencyPressure-cookersEngineeringEnergy conservation
The invention relates to a high-strength multifunctional pressure-bearing pot cover. A main body, an arc-shaped groove plate, a main cover handle, a manual valve, an automatic valve, a main cover body, a pot edge groove, a movable rod, a movable rod clip, a movable shaft, sealing bolts and a handle fixing nail are organically arranged, wherein the arc-shaped groove plate is arranged in an arc-shaped plate on the upper end of the pot edge groove and in a hollow-out arc-shaped groove shape; the main cover handle is placed in the upper side of the main cover body; the manual valve is hidden in the main cover handle; an inlet and an outlet respectively communicate with the lower side of the main cover body and the lower side of the main cover handle; the automatic valve is hidden into the main cover handle; an inlet and an outlet respectively communicate with the lower side of the main cover body and the lower side of the main cover handle; the main cover body is arranged in an end port of a pressure cooker and in the pot edge groove; the pot edge groove is arranged in the pressure cooker end port and the lower side of the main cover body; the movable rod is disposed in the arc-shaped groove plate; the movable rod clip is disposed in a movable rod recessed pit; the inner side of the movable shaft is connected with one side of the main cover body via the fixing nail; the sealing bolts are symmetrically arranged on the lower side of the main cover body; and the handle fixing nail is hidden into the main cover handle. Therefore, the high-strength multifunctional pressure-bearing pot cover can be safely used and has obvious comprehensive energy conservation effect.
Owner:LIUZHOU JINGYANG ENERGY SAVING TECH RES DEV

Temperature-controlled crack prevention construction method for concrete structure

The invention discloses a temperature-controlled crack prevention construction method for a concrete structure. The method comprises the steps of (1) arranging temperature probes on the surface of a large-size concrete pouring block to measure the temperature difference between inside and outside, the cooling rate of the large-size concrete pouring block and the environment temperature; (2) establishing a calculation model for the temperature-controlled construction scheme based on the obtained measuring result; (3) collecting the construction site parameters, and inputting the parameters into the obtained calculation model for temperature-controlled simulation calculation; and (4) comparing the temperature-controlled simulation calculation result obtained in the step (3) with the preset auxiliary expert system, repeating the step (2) to adjust the corresponding parameters when the temperature-controlled simulation calculation result obtained in the step (3) and the preset auxiliary expert system mismatch, and optimizing the temperature-controlled crack prevention construction scheme for concrete preset based on experience until the optimal temperature-controlled crack prevention construction scheme for the concrete is obtained. The temperature-controlled crack prevention construction method for the concrete structure disclosed by the invention has the advantages that the concrete is not prone to crack, the crack prevention reliability is high, and the crack prevention commonality is good.
Owner:JINLAI CONSTR ENG TECH RES & DEV CO LTD OF THE XINJIANG PRODION & CONSTR CORPS

Starting method of reaction-regenerative device for preparing low carbon olefin form methanol

The invention relates to a starting method for a reaction-regeneration device which uses methanol to prepare low-carbon olefin, mainly comprising the following steps: a. using an auxiliary combustion chamber to heat air, and then entering the reaction-regeneration device; heating the dense phase temperature of a regenerator to 400-600 DEG C, and heating the temperature of a reactor reaction zone to 150-350 DEG C; b. switching the catalyst from a catalyst storage tank into the regenerator, and injecting the combustion oil to maintain the temperature of the regenerator; c. switching the catalyst from the regenerator into the reactor, and establishing reaction catalyst circulation between the reactor and the regenerator; d. heating the reactor reaction zone to a temperature not less than 350 DEG C, and putting the raw materials containing the methanol in the reactor to contact with the catalyst so as to generate the products containing low-carbon olefin and also form a carbon deposit on the catalyst; e. stop injecting combustion oil to the regenerator; f. stop using the auxiliary combustion chamber. The method has short starting period and light catalyst damage degree, which can be used for low-carbon olefin industrial production.
Owner:CHINA PETROLEUM & CHEM CORP +1

Selectivity hydrogenation method for whole fraction crack petroleum

The invention relates to a method for selective hydrogenation of full-run pyrolysis gasoline, which mainly solves the technical problem in the prior art that it is difficult to selectively hydrogenate full-run pyrolysis gasoline with high colloid and free water content. The present invention adopts the pyrolysis gasoline and hydrogen of the hydrocarbon compound fraction with C5 hydrocarbon to dry point of 204 DEG C as raw materials, the reaction temperature is 30 to 80 DEG C, the reaction pressure is 2.0 to 3.0 MPa, and the fresh oil space velocity is 2.5 to 5.0 hour-1, under the condition that the hydrogen/oil volume ratio is 60-120:1, the raw material is contacted with the catalyst and reacts to convert the diolefin and alkenyl aromatic components in the raw material into monoolefin and alkylaromatic. Including alumina support, active component metal palladium or its oxide, at least one element selected from IA or IIA in the periodic table or its oxide, at least one element selected from IVA or VA in the periodic table or its oxide Oxide, the specific surface area of ​​the carrier is 40-160 m2/g, the total pore volume is 0.3-1.2 ml/g, and the carrier has a technical solution of composite pore distribution, which solves this problem well and can be used for full-run pyrolysis gasoline In the industrial production of selective hydrogenation.
Owner:CHINA PETROLEUM & CHEM CORP +1

Organic silicon micro-pore zeolite and synthesizing method thereof

The present invention relates to a silicone microporous zeolite and the synthesis method of the silicone microporous zeolite, used to solve the problem that a frame structure of the microporous zeolite synthesized by the prior technology does not contain the silicone and to provide the microporous zeolite, in which the frame structure contains the silicone. The present invention contains the following mol relation: In the formula of (1/n) Al2O3: SiO2: (m/n) R, n is equal to 5-1000 and m is equal to 0.01-300. R is an alkyl, an alkane alkenyl or a phenyl. A solid nuclear magnetic map of Si29NMR is between -80ppm and +50ppm and includes at least one nuclear magnetic resonance spectral peak of Si29. A diffraction pattern of x-ray has a d-spacing maximum at the position of 11.14 plus or minus 0.05, 9.99 plus or minus 0.05, 9.74 plus or minus 0.05, 6.36 plus or minus 0.05, 5.99 plus or minus 0.05, 5.70 plus or minus 0.05, 5.57 plus or minus 0.05, 4.98 plus or minus 0.05, 4.26 plus or minus 0.05, 3.83 plus or minus 0.05, 3.75 plus or minus 0.05, 3.72 plus or minus 0.05, 3.65 plus or minus 0.05, 3.44 plus or minus 0.05, 3.32 plus or minus 0.05 angstrom and 3.05 plus or minus 0.05 angstrom. The microporous zeolite can serve as a sorbent or an activator component used in the transformation of the organic compounds.
Owner:CHINA PETROLEUM & CHEM CORP +1

Catalyst for producing low-carbon olefin by using synthesis gas and preparation method of catalyst

The invention relates to a catalyst for producing low-carbon olefin by using synthesis gas and a preparation method of the catalyst, and is mainly used for solving the problem of low CO conversion rate and low low-carbon olefin selectivity in reaction for preparing the low-carbon olefin by using the synthesis gas in the prior art. The catalyst consists of a composite carrier and active components, wherein the composite carrier consists of alpha-aluminium oxide and a ZSM-5 molecular sieve; the silicon-aluminium ratio of the ZSM-5 molecular sieve is 40-200; the active components are loaded on the composite carrier and comprise the following compounds with chemical formulas by atomic ratio: Fe100AaBbCcOx, A is at least one of transition metals of Cu and Mn, B is at least one of lanthanide La and Ce, and C is at least one of alkaline metals of K and Cs; the weight of the composite carrier is 20%-80% of the weight of catalyst; by weight percent of the composite carrier, the weight of alpha-aluminium oxide is 20%-99% of the weight of the composite carrier. With the adoption of the technical scheme, the problem is well solved; the catalyst can be used for industrial production of the low-carbon olefin produced by using the synthesis gas.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for preparing p-xylene by separating and crystallizing mixed xylenes

The invention relates to a method for preparing p-xylene by separating and crystallizing mixed xylenes, and mainly solves the problem of large energy consumption in a crystal separating process in the prior art. To well solve the problem, the invention adopts the following technical scheme of preparing the p-xylene by separating and crystallizing the mixed xylenes that: p-xylene crystal I and crystallization filtered stock I are obtained by crystallizing mixed xylenes in a primary crystallizer and separating crystal mush; the crystal I is melted by heat exchange, is partially returned to a first solid-liquid separator, and partially enters a product tank; the crystallization filtered stock I is separated into two streams, one stream returns to the crystallizer, and the other stream entersa pulping tank; one part of crystal mush in the primary crystallizer is cleared so as to obtain clear crystallization stock I which enters the pulping tank; p-xylene crystal II and crystallization filtered stock II are obtained by separating the crystal mush in a secondary crystallizer by a second solid-liquid separator; the crystal II enters the pulping tank, and separated after mixed heat exchange so as to obtain p-xylene crystal III and crystallization filtered stock III; the crystal III is melted by heat exchange, is partially returned to a third solid-liquid separator to be used as cleaning solution, and partially enters the product tank; the crystallization filtered stock II is separated into two streams, one stream returns to the secondary crystallizer, and the other stream enters the pulping tank; the crystallization filtered stock II and the mixed xylenes are subject to heat exchange and enter a stock tank; and the clear crystallization stock II and the mixed xylenes are subjected to heat exchange and enter the stock tank. The method can be used in p-xylene industrial production.
Owner:CHINA PETROLEUM & CHEM CORP +1

Polydisperse polyacrylamide microsphere system and preparation method thereof

ActiveCN106866880AHigh effective solid contentSatisfies the characteristics of severely heterogeneous strataDrilling compositionPolymer scienceMicrosphere
The invention relates to a polydisperse polyacrylamide microsphere system and a preparation method thereof. The invention mainly overcomes the problem that nanometer, micrometer and millimeter polyacrylamide microspheres cannot be prepared in a same system in the prior art. The preparation method comprises the following steps: preparing nanometer polymer microspheres by using a multi-step polymerization method according to the mechanism of reversed-phase microemulsion polymerization; then supplementing a water phase, adjusting a ratio of an oil phase to an emulsifier to the water phase and the usage amount of an initiator and synthesizing submicron polymer microspheres according to the mechanism of reversed-phase emulsion polymerization; and supplementing the water phase and the initiator and continuing synthesis of micrometer to millimeter polymer particles. Thus, the above-mentioned problem is overcome; and the prepared polydisperse polyacrylamide microsphere system has the characteristics of high effective solid content, inclusion of nanometer, micrometer and millimeter polymer microspheres and capacity of meeting requirements of severe heterogeneous formations, and can be directly used or cooperatively used with other oil-field chemicals on site for in-depth profile control, water plugging, oil displacement or other recovery-efficiency-improving operations for tertiary oil recovery in an oil field.
Owner:CHINA PETROLEUM & CHEM CORP +1
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