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30results about How to "High removal depth" patented technology

Metal-modified 13X molecular sieve desulphurization adsorbent and its preparation method and use

The invention relates to a metal-modified 13X molecular sieve desulphurization adsorbent and its preparation method and use. The preparation method comprises preparing a metal salt solution as an active ingredient ion exchange salt solution for next use, taking a 13X molecular sieve, adding the 13X molecular sieve into the ion exchange salt solution for ion exchange reaction, carrying out filtration, washing the filter residues, carrying out drying, putting the dried filter residues into a tube furnace, carrying out roasting activation, and carrying out furnace cooling to obtain the molecular sieve desulphurization adsorbent subjected to metal ion exchange. The molecular sieve desulphurization adsorbent can be used for ultra-deep removal of sulfocompounds such as thiophene and its derivatives in gasoline and diesel oil. The metal-modified 13X molecular sieve desulphurization adsorbent has a large specific surface area and a rich micropore structure, can effectively remove a trace amount of sulfocompounds in gasoline, has the advantages of low cost, simple preparation processes, high removal depth and regeneration convenience, can be used for deep removal of sulfocompounds in fuel oil products and preparation of ultral-low sulphur clean fuel oil, reduces oil product combustion sulfide discharge-caused environmental pollution and improves environment quality.
Owner:SHANGHAI RES INST OF CHEM IND

Residual oil hydrogenation treatment and catalytic cracking combination method

The present invention discloses a residual oil hydrogenation treatment and catalytic cracking combination method. According to the method, the residual oil hydrogenation treatment process comprises two hydrogenation protection reactors, wherein the two hydrogenation protection reactors are arranged in parallel connection, the feed material of the first hydrogenation protection reactor is the residual oil raw material, and the feed material of the second hydrogenation protection reactor is the catalytic cracking heavy fraction; the effluents of the two reactors are mixed, and the resulting mixture enters a hydrogenation treatment reaction zone to carry out a hydrogenation reaction; the effluent of the hydrogenation reaction is subjected to gas-liquid separation, wherein the resulting gas phase is circularly adopted for the hydrogenation reaction, and the liquid phase directly enters a catalytic cracking apparatus without fractionation; the effluent of the catalytic cracking reaction is separated to obtain dry gas, liquefied gas, catalytic cracking gasoline, and catalytic cracking heavy fraction after catalytic cracking of the gasoline, wherein the catalytic cracking heavy fraction is adopted as the feed material of the second hydrogenation protection reactor. With the method, the operating period of the residual oil hydrogenation apparatus can be prolonged, the maximum amount of the catalytic cracking gasoline can be produced, and the equipment investment can be saved.
Owner:CHINA PETROLEUM & CHEM CORP +1

System for removing heat-stable salt in organic amine liquid and method

The invention relates to the field of purification of organic amine liquid, and discloses a system for removing a heat-stable salt in organic amine liquid and a method for treating the organic amine liquid by adopting the system. The system comprises an organic amine liquid storage device, an electrode liquid storage device, a desalting water storage device and a membrane stack, wherein the membrane stack communicates with the organic amine liquid storage device, the electrode liquid storage device and the desalting water storage device separately, and an organic amine liquid circulation loop,an electrode liquid circulation loop and a desalting water circulation loop are formed separately, the system further comprises conductivity meters and a control center, and the control center is used for receiving conductivity signals from the conductivity meters, and for adjusting circulation flows of the organic amine liquid circulation loop and the desalting water circulation loop, reuse of the organic amine liquid and discharge of waste liquid according to the conductivity signals of the conductivity meters. When the organic amine liquid is treated by the system, anions and cations in the amine liquid can be removed synchronously, so that consumption of alkali liquid and discharge of the waste liquid are reduced.
Owner:BEIJING SIJIANTONG TECH&DEV

Production method comprehensively utilizing high-zinc cobalt raw materials

The invention relates to a production method comprehensively utilizing high-zinc cobalt raw materials. The method comprises the following steps that firstly, the high-zinc cobalt raw materials are subjected to reduction leaching, soluble valuable metals such as zinc and cobalt enter a solution, and solid-liquid separation is conducted; secondly, after solid-liquid separation, the solution is subjected to deironing through a jarosite method, the PH value is adjusted to 4.7+/-0.2 at the same time, aluminum in the solution is precipitated to be removed in an aluminum hydroxide mode, and solid-liquid separation is conducted; and thirdly, the solution enters a P507 extraction tank, 20%-30% of a P507 extraction agent is adopted, caustic soda liquid is added, the saponification rate is controlled to be 50-60%, Zn2+ in the solution is extracted into organic phases, the organic phases are washed through dilute sulfuric acid, other metal ions are co-extracted and washed down, then the organic phases are subjected to reverse extraction, the Zn2+ enters aqueous phases from the organic phases through reverse extraction by means of a dilute sulfuric acid solution, and a high-purity zinc sulfate solution is generated, concentrated and crystallized into zinc sulfate monohydrate crystals.
Owner:GEM JIANGSU COBALT IND CO LTD

Process for separating copper in nickel-cobalt-copper system by solvent extraction method

The invention provides a process for separating copper in a nickel-cobalt-copper system by a solvent extraction method. The process comprises the following steps: by taking N902-sulfonated kerosene as an extracting agent, controlling the volume ratio of an organic phase to a water phase at (3:1) to (4:1); regulating the pH value of a material liquid to 2.0-2.5; extracting at room temperature; and after carrying out clearing and phase separation on raffinate, based on sulfuric acid as a reverse extraction acid for the copper-supported organic phase, controlling the volume ratio of the organic phase to the reverse extraction acid at (6:1)-(4:1), carrying out reverse extraction at room temperature, and eluting a reverse extraction liquid to obtain a copper sulfate solution. In the process, the N902-sulfonated kerosene is used as the extracting agent, sulfuric acid is used as a reverse extraction agent, copper is separated out of the high-concentration nickel-cobalt-copper system in a high selectivity and high reverse extraction property mode, and copper is output in a pure copper sulfate solution form, thereby avoiding the retreatment and recovery of copper slag with a chemical method, and the recovery of copper is high; and after nickel-cobalt raffinate with copper removed is subjected to sodium jarosite iron removal, P204 deep impurity removal and P507 separation of nickel-cobalt, nickel-cobalt salt products are produced, thereby achieving the purification and separation of copper in a nickel-cobalt-copper impure material and the comprehensive recovery of nickel-cobalt-copper.
Owner:JINCHUAN GROUP LIMITED

Preparation method of ammonium bifluoride

The invention discloses a preparation method of ammonium bifluoride. The method comprises steps as follows: a, dilute ammonia water and ammonium bifluoride mother liquor are mixed to adsorb gas containing fluorine and silicon, and a mixed solution is obtained; b, the mixed solution and filter-press residues obtained in Step d are mixed for slurry making and filter-press separation, and a filtrate and a silica by-product are obtained; c, ammonia is introduced into the filtrate; d, slurry is subjected to filter-press separation, and an ammonium fluoride filtrate and filter-press residues are obtained; e, the ammonium fluoride filtrate is subjected to vacuum concentration; f, concentrated slurry is dissolved, the pH value of the solution is adjusted with hydrogen fluoride, and cooling crystallization is performed; g, ammonium bifluoride crystals are filtered, separated and dried, and the ammonium bifluoride product is obtained. With the adoption of the method, the utilization rate of fluorine and ammonia is increased, the gas containing fluorine and silicon is changed into the ammonium bifluoride product with the high economic value in the phosphoric acid production process, the production cost is low, the economic benefit is significant, meanwhile, the purity and other indexes of the product meet the requirement for superior products, and the method is suitable to be popularized and applied in the field.
Owner:GUIZHOU CHANHEN CHEM CO LTD

Combined process of hydrotreatment and light fraction-conversion for residual oil

ActiveCN103102944BImprove the effect of hydrotreating reactionAct as a diluentTreatment with hydrotreatment processesFluidized bedFixed bed
The invention discloses a combined process of hydrotreatment and light fraction-conversion for residual oil. The combined process comprises the following steps: (1) allowing an inferior heavy oil feedstock to enter into a solvent deasphalting device so as to obtain deasphalted oil and de-oiled asphalt; (2) mixing the de-oiled asphalt obtained in step (1) with at least a part of oil slurry and allowing an obtained mixture to enter into a fluidized bed hydrotreatment unit for fluidized bed hydrotreatment; (3) mixing an effluent of fluidized bed hydrotreatment obtained in the step (2) with the deasphalted oil, adding at least a part of recycle oil of a catalytic cracking unit at the same time and allowing an obtained mixture to enter into a fixed bed hydrotreatment unit, wherein generated oil of an effluent of fixed bed hydrotreatment is used as a feedstock for the catalytic cracking unit; and (4) carrying out treatment in a fractionating tower of the catalytic cracking unit so as to obtain catalytic cracking reaction products including a gasoline fraction, a diesel oil fraction, recycle oil and oil slurry. Compared with the prior art, the combined process provided by the invention has the advantages of wide sources of the feedstocks, low equipment investment, stable operation, a long operation period and a good synergistic and coordination effect.
Owner:CHINA PETROLEUM & CHEM CORP +1

Green smelting method based on rhodochrosite leaching-purification

The invention belongs to the field of manganese metallurgy, and particularly discloses a green smelting method based on rhodochrosite leaching-purification. The method adopts a two-stage reverse feeding countercurrent leaching process, namely in the first-stage leaching process, rhodochrosite slurry is used as a base solution, anolyte, sulfuric acid solution or acid leaching solution is added into the base solution, the terminal pH is controlled to be greater than or equal to 4.5, and the manganese leachate with low impurity content can be obtained; in the second-stage leaching process, first-stage leaching residues serve as raw materials, anolyte or sulfuric acid solution is added into the first-stage leaching residues, the terminal pH is controlled to be smaller than or equal to 1.5, so that manganese in the first-stage leaching residues is thoroughly extracted, second-stage leaching residues low in manganese content and acid leaching liquid are obtained, the acid leaching liquid is returned to the first-stage to be used for leaching, and the second-stage leaching residues are washed and then sent to a residue field to be piled up or serve as mine filling materials; and through the leaching process, the separation of impurities can be realized, the manganese resource can be fully utilized, and the consumption of acid and alkali is reduced. The method has the advantages of simple process, low cost, high manganese recovery rate, low auxiliary material consumption and the like, and has a good industrial application prospect.
Owner:AKETAO KEBANG MANGANESE IND MFG CO LTD +1

Residual oil conversion combined process method

The invention discloses a combined process for conversion of residual oil. The combined process comprises the following steps: (1) allowing a residual oil raw material to enter into a solvent deasphalting unit so as to obtain deasphalted oil and de-oiled asphalt; (2) mixing the de-oiled asphalt obtained in step (1) with heavy distillate oil of a catalytic cracking unit and allowing an obtained mixture to enter into a fluidized bed hydrotreatment unit for fluidized bed hydrotreatment; (3) mixing an effluent of fluidized bed hydrotreatment obtained in the step (2) with the deasphalted oil and carrying out fixed bed hydrotreatment, wherein generated oil of an effluent of fixed bed hydrotreatment is used as a raw material for the catalytic cracking unit; and (4) mixing the de-oiled asphalt with a catalytic heavy fraction obtained after dry gas, liquefied gas and catalytic gasoline are separated from an effluent of a catalytic cracking reaction and subjecting an obtained mixture to fluidized bed hydrotreatment. Compared with the prior art, the combined process provided by the invention has the advantages of wide sources of the raw materials, low equipment investment, stable operation, a long operation period and a good synergistic and coordination effect.
Owner:CHINA PETROLEUM & CHEM CORP +1

Adsorbent for deeply removing carbon monoxide in hydrogen, preparation method of adsorbent and method for removing carbon monoxide in hydrogen by adopting adsorbent

An adsorbent for deeply removing trace carbon monoxide in hydrogen comprises an active component and a high-specific-surface-area active carbon carrier loading the active component, and the active component is a monovalent copper or bivalent copper compound. The preparation method comprises the following steps of: (1) dissolving an active component precursor in water, and fully stirring to obtain a precursor solution; (2) dispersing and impregnating an activated carbon carrier with a high specific surface area by using the obtained precursor solution; (3) integrally drying the impregnated carrier and the precursor solution at the temperature of 40-100 DEG C; and (4) sintering the dried carrier in an inert atmosphere at the temperature of 150-300 DEG C for 3-6 hours to obtain the adsorbent. The adsorbent is uniform in active component dispersion, high in removal depth, high in selectivity, large in capacity, low in activation temperature, easy to regenerate and suitable for deeply removing carbon monoxide in hydrogen fuel of a fuel cell. The preparation method is simple in process, low in cost, free of active component loss in the preparation process and easy to industrially amplify.
Owner:CHINA PETROLEUM & CHEM CORP +1

Residual oil hydrogenation treatment and catalytic cracking combination method

The present invention discloses a residual oil hydrogenation treatment and catalytic cracking combination method. According to the method, the residual oil hydrogenation treatment process comprises two hydrogenation protection reactors, wherein the two hydrogenation protection reactors are arranged in parallel connection, the feed material of the first hydrogenation protection reactor is the residual oil raw material, and the feed material of the second hydrogenation protection reactor is the catalytic cracking heavy fraction; the effluents of the two reactors are mixed, and the resulting mixture enters a hydrogenation treatment reaction zone to carry out a hydrogenation reaction; the effluent of the hydrogenation reaction is subjected to gas-liquid separation, wherein the resulting gas phase is circularly adopted for the hydrogenation reaction, and the liquid phase directly enters a catalytic cracking apparatus without fractionation; the effluent of the catalytic cracking reaction is separated to obtain dry gas, liquefied gas, catalytic cracking gasoline, and catalytic cracking heavy fraction after catalytic cracking of the gasoline, wherein the catalytic cracking heavy fraction is adopted as the feed material of the second hydrogenation protection reactor. With the method, the operating period of the residual oil hydrogenation apparatus can be prolonged, the maximum amount of the catalytic cracking gasoline can be produced, and the equipment investment can be saved.
Owner:CHINA PETROLEUM & CHEM CORP +1

Building internal wall waterproof formaldehyde-removing coating applied to indoor environment as well as manufacturing method thereof

The invention discloses a building internal wall waterproof formaldehyde-removing coating applied to an indoor environment as well as a manufacturing method thereof. The waterproof formaldehyde-removing coating comprises three parts, namely a component A, a component B and a component C, wherein the component A is prepared by putting sawdust and green straws under the comprehensive action of cellulase, pectinase and diluted hydrochloric acid to obtain a viscous solution, performing high-temperature sterilization, performing neutralizing treatment by using alkali in an amount which is smaller than that of acid and finally implanting bacillus thuringiensis to cultivate; the component B is obtained by suspending an activated carbon micropowder, a 1000-mesh ash calcium powder and a 1000-mesh triple superphosphate powder into absolute ethanol; and the component C is formed by performing enzymolysis and alcohol washing on the sawdust and the green straws and dehydrating the remaining by using the cellulose taking lignin as a main material. The building internal wall waterproof formaldehyde-removing coating has a spontaneous respiration like property, a durable formaldehyde-removing effect and high removing depth, is green, pollution-free and water-resistant, and can consume water.
Owner:山东天汇防水股份有限公司

Multivariate highly active component carbon monoxide adsorbent and its preparation method and application

The invention relates to a multi-element high-activity component carbon monoxide adsorbent as well as a preparation method and application thereof. The multi-element high-activity component carbon monoxide adsorbent is mainly prepared by an active component co-precipitation method; an active component comprises high-valence oxide of Cu, Zn, Mn, Ni and Fe: CuO, ZnO, MnOx, NiO and FeOy as well as dispersing agent Al2O3 powder. The multi-element high-activity component carbon monoxide adsorbent as well as the preparation method and application thereof have the benefits that by utilizing the characteristic of complementary performances of different components, the multiple components reach high-valence states through oxidation, and further, the ability to remove carbon monoxide by chemical adsorption is realized; the effect of a catalyst of the multi-element high-activity component carbon monoxide adsorbent is superior to that of a single or two-component catalyst; the multi-element high-activity component carbon monoxide adsorbent has the advantages of being free from loss of effective component of feed gas, high in removal depth, large in capacity, low in activation temperature, strong in anti-sintering ability, long in service life, high in mechanical strength, hard to pulverize and the like, is suitable for C2H4, C3H6, CH4, H2, N2, He, Ne, Ar, Kr, Xe and deep removal of the carbon monoxide by electron gas, and can be widely applied to large-scale industrial production.
Owner:大连圣得环保新材料有限公司

A kind of preparation method of ammonium bifluoride

The invention discloses a preparation method of ammonium bifluoride. The method comprises steps as follows: a, dilute ammonia water and ammonium bifluoride mother liquor are mixed to adsorb gas containing fluorine and silicon, and a mixed solution is obtained; b, the mixed solution and filter-press residues obtained in Step d are mixed for slurry making and filter-press separation, and a filtrate and a silica by-product are obtained; c, ammonia is introduced into the filtrate; d, slurry is subjected to filter-press separation, and an ammonium fluoride filtrate and filter-press residues are obtained; e, the ammonium fluoride filtrate is subjected to vacuum concentration; f, concentrated slurry is dissolved, the pH value of the solution is adjusted with hydrogen fluoride, and cooling crystallization is performed; g, ammonium bifluoride crystals are filtered, separated and dried, and the ammonium bifluoride product is obtained. With the adoption of the method, the utilization rate of fluorine and ammonia is increased, the gas containing fluorine and silicon is changed into the ammonium bifluoride product with the high economic value in the phosphoric acid production process, the production cost is low, the economic benefit is significant, meanwhile, the purity and other indexes of the product meet the requirement for superior products, and the method is suitable to be popularized and applied in the field.
Owner:GUIZHOU CHANHEN CHEM CO LTD
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