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51 results about "Diisobutylketone" patented technology

Method for separating zirconium and hafnium

The invention relates to a method for separating zirconium and hafnium, which specifically comprises the following steps of: using the acidic water solution of a zirconium compound as a raw material, extracting hafnium in the material liquid into an organic phase by using diisobutyl ketone (DIBK) or the synergism of DIBK with a neutral phosphorous extracting agent or the synergism of DIBK with anacidic phosphorus-containing extracting agent, and washing and stripping the oganic phase to produce a hafnium-rich liquid such that the separation of zirconium and hafnium is realized; respectively precipitating the hafnium-rich liquid and the remaining organic phase by using ammonia water, and washing and roasting the precipitates to obtain atomic energy level zirconium oxide and hafnium oxide.In the technical method provided by the invention, low content of hafnium in zirconium hafnium is preferably extracted, and the method has simple process and high extraction efficiency. The extraction system used in the method reaches the same zirconium and hafnium separation performance to MIBK (Methyl Isobutyl Ketone) but has smaller water solubility, high boiling point and flashing point and smaller toxicity compared with MIBK, and the problems of great solvent loss, easy outbreak of fire, environmental pollution and the like in the MIBK extraction separation method are solved.
Owner:有研资源环境技术研究院(北京)有限公司

Application of inorganic alkaline and fixed-bed adsorption technique to deacidification and purification of diisobutyl ketone

The invention relates to an inorganic alkaline adsorbing agent for deacidification and purification of diisobutyl ketone, a preparation method and a fixed-bed adsorption technique, which belong to the field of fine chemical engineering. The adsorbing agent comprises organic alkaline substances accounting for 70-90% of the overall weight of the adsorbing agent. The preparation method is characterized in that the organic alkaline substances are used as carriers, adhesives, pore-enlarging additives and an appropriate amount of deionized water are added and proportionally mixed, and then the adsorbing agent is obtained by means of forming, drying and sintering. A fixed-bed adsorption column is added to a product outlet of a diisobutyl ketone production device and operated at the normal temperature and under the normal pressure, and the inorganic alkaline adsorbing agent can be regenerated by means of high-temperature sintering and reused for 8-10 times. The content of free acid in the diisobutyl ketone is reduced from 0.05% to less than or equal to 0.02%. The technique effectively meets the requirements which cannot be met by a traditional method, and has the advantages that equipment investment is low, raw materials are easy to obtain, the technique is simple, material loss is low and the like. Waste water is avoided in inorganic alkaline adsorbing agent preparation, deacidification and purification and adsorbing agent regeneration techniques.
Owner:JILIN INST OF CHEM TECH

Preparation method of catalyst for co-generating of isopropanol and diisobutyl ketone through acetone hydrogenation and application

The invention provides a preparation method of a catalyst for co-generating of isopropanol and diisobutyl ketone through acetone hydrogenation and an application. The preparation method is characterized in that the catalyst comprises an alumina carrier as well as Ni and Mg loaded on the gamma-Al2O3 carrier; in terms of total weight of the catalyst, the catalyst comprises 20-25% of Ni and 8-12% of Mg; the preparation method comprises the following procedures of 1) carrier preparation: taking a pseudo-boehmite powder body; adding a certain quantity of adhesives and extrusion assisting agents to the pseudo-boehmite powder body; extruding a mixture into strips or rotationally granulating the mixture; and drying and roasting the mixture so as to obtain the carrier; 2) impregnation of magnesium nitrate and nickel nitrate: impregnating the carrier in the magnesium nitrate and the nickel nitrate for 10-24 hours at room temperature; taking out the carrier after filtering the carrier; drying and roasting the carrier; and then naturally cooling the carrier; and 3) repeating of the step 2): using a magnesium nitrate and nickel nitrate impregnation liquor obtained in the step 2); impregnating a semi-finished product obtained in the step 2) in the impregnation liquor; and repeating the impregnating, drying and roasting process for at least three times according to the step 2) so as to obtain a catalyst finished product. The invention further relates to a catalytic application of the catalyst, which is prepared by the preparation method, used for co-generating the isopropanol and the diisobutyl ketone through acetone hydrogenation.
Owner:CHINA NAT OFFSHORE OIL CORP +1

Technique for preparing MIBK (methyl isobutyl ketone) from acetone with liquid-phase one-step process

The invention provides a technique for preparing MIBK (methyl isobutyl ketone) from acetone with a liquid-phase one-step process. The technique comprises the following steps: hydrogen and acetone are fed into a reactor and subjected to a reaction under catalysis of gamma-Al2O3 doped hydrogen-type polystyrene cation exchange resin, and a product is delivered to an acetone recovery tower for separation; organic light components in the recovery tower are delivered to a wastewater tower, acetone is delivered back to the reactor, and heavy components at the tower bottom are delivered to a water removal tower; light components at the top of the water removal tower are delivered to an extraction tower, and a reaction product at the tower bottom is delivered to a finished product tower; purified water is adopted as an extracting agent in the extraction tower, and heavy components are delivered to the wastewater tower; MIBK is produced from a side line of the finished product tower, 2,6-dimethyl-4-heptanone and high-class ketone are produced from a tower bottom liquid. The technique is short in flow and low in energy consumption, 2,6-dimethyl-4-heptanone is co-produced, few noble metal palladium active components in a palladium supported resin catalyst are lost, stable service life as long as 7,000 h is realized, and the production cost is reduced.
Owner:湖北三里枫香科技有限公司

Catalyst used for preparing methyl isobutyl ketone and diisobutyl ketone by acetone condensation as well as preparation method and application of catalyst

The invention relates to a catalyst used for preparing methyl isobutyl ketone and diisobutyl ketone by acetone condensation as well as a preparation method and application of the catalyst, and belongsto the field of acetone condensation catalysts. The catalyst used for preparing the methyl isobutyl ketone and the diisobutyl ketone by the acetone condensation comprises the following components, inpercentages by weight: (1) 2%-25% of copper or an oxide of the copper, (2) 8%-35% of zinc or an oxide of the zinc, (3) 2%-40% of cobalt or an oxide of the cobalt, (4) 1%-10% of barium or an oxide ofthe barium, (5) 30%-80% of aluminum oxide, and (6) 1%-40% of silicon dioxide. The catalyst provided by the invention uses the copper, the zinc, the cobalt and the like as loading components, the balance of acidity and alkalinity of the catalyst is properly adjusted, and the catalyst with a suitable catalyst pore structure is prepared; the catalyst is used at a lower reaction temperature, and has avery high conversion rate of acetate, less by-products, a high product yield, and low subsequent separation energy consumption; and after long-term evaluation, the catalyst shows ideal stability.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for preparing diisobutyl ketone

The invention discloses a method for preparing diisobutyl ketone. The method comprises the following steps: 1, transferring a mixture raw material extracted from a tower kettle of a methyl isobutyl ketone light component tower and mainly containing diisobutyl ketone into a reaction tank; 2, adding a silica-gel drier into the reaction tank, and performing stirring at rotating speed of 100 revolutions/min; 3, filtering the mixture raw material in the reaction tank by virtue of a filter; 4, delivering filtrate obtained by filtration into a preheater for preheating at preheating temperature of 76 to 94 DEG C; 5, delivery the preheated filtrate into a rectification tower for rectification, wherein the temperature of the top of the tower is controlled to be 104 to 126 DEG C, the side stream temperature is 156 to 177 DEG C, and the temperature of a tower kettle is 167 to 189 DEG C; 6, producing a diisobutyl ketone finished product from a side stream of the rectification tower, and charging the diisobutyl ketone finished product. According to the method, the temperature difference of boiling points of each substance is increased, and the rectification efficiency of the rectification tower is favorably improved, so that the purity of the diisobutyl ketone is improved on the premise of simplifying a purification process, and the economic benefits of the diisobutyl ketone are further greatly improved.
Owner:ZHEJIANG OCEANKING DEVELOPMENT CO LTD

Method for separating zirconium and hafnium

The invention relates to a method for separating zirconium and hafnium, which specifically comprises the following steps of: using the acidic water solution of a zirconium compound as a raw material, extracting hafnium in the material liquid into an organic phase by using diisobutyl ketone (DIBK) or the synergism of DIBK with a neutral phosphorous extracting agent or the synergism of DIBK with anacidic phosphorus-containing extracting agent, and washing and stripping the oganic phase to produce a hafnium-rich liquid such that the separation of zirconium and hafnium is realized; respectively precipitating the hafnium-rich liquid and the remaining organic phase by using ammonia water, and washing and roasting the precipitates to obtain atomic energy level zirconium oxide and hafnium oxide.In the technical method provided by the invention, low content of hafnium in zirconium hafnium is preferably extracted, and the method has simple process and high extraction efficiency. The extraction system used in the method reaches the same zirconium and hafnium separation performance to MIBK (Methyl Isobutyl Ketone) but has smaller water solubility, high boiling point and flashing point and smaller toxicity compared with MIBK, and the problems of great solvent loss, easy outbreak of fire, environmental pollution and the like in the MIBK extraction separation method are solved.
Owner:有研资源环境技术研究院(北京)有限公司
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