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124 results about "Alkyne formation" patented technology

In organic chemistry, an alkyne is an unsaturated hydrocarbon containing at least one carbon—carbon triple bond. The simplest acyclic alkynes with only one triple bond and no other functional groups form a homologous series with the general chemical formula CnH2n−2.

Composite metal oxide loading active metal catalyst and preparation method thereof

The invention provides a composite metal oxide loading active metal catalyst and a preparation method thereof. The catalyst is formed by loading an active metal component by a composite metal oxide serving as a carrier. The catalyst has the characteristics that the active metal component is highly and stably dispersed on the surface of the carrier, the crystal shape is complete, the size is uniform, the particle size is 1 to 5 nm, and the particle size distribution range is small. The preparation method provided by the invention comprises the following steps: dissolving two or three soluble metal salts in deionized water to prepare a mixed salt solution, mixing the mixed salt solution with an alkaline precipitator, and carrying out crystallizing, washing, drying and roasting to obtain a composite metal oxide carrier which is of a uniform microspherical structure and has an average diameter of 0.3 to 3.0 [mu]m; steeping the carrier in steeping liquid to enable the carrier to be coated with the metal salts, and carrying out drying, roasting and reduction to obtain the catalyst. The catalyst can be applied to various alkyne hydrogenation reaction processes in the fields of petrochemical engineering, fine chemical engineering and the like, and is outstanding in catalysis property and easy to recycle and reuse.
Owner:BEIJING UNIV OF CHEM TECH

Selective hydrogenation method of acetylene hydrocarbon and dialkene in cracking gas

The invention discloses a selective hydrogenation method for acetylene hydrocarbon and diene in pyrolysis gas and belongs to the technical field of selective hydrogenation of unsaturated hydrocarbon. In order to solve the problems in the prior art of high energy consumption, large equipment size, high operation cost, incapable of improvement of C3 selectivity, and the like, due to the facts that liquid phase flow of a mixed phase hydrogenation reactor contains a large amount of C3, C4 and C5 components, can not realize full rinse in the reactor, and repeatedly enters into a front depropanizing tower. The invention provides the method which comprises: carrying out preferential selective hydrogenation of C2-C10 highly unsaturated hydrocarbon (acetylene hydrocarbon and diene) on the upstream of the front depropanizing tower; condensing heavy components above C6 through dephlegmation; and using the heavy components as the fluid phase flow of the mixed phase hydrogenation reactor. The method makes full use of the liquid phase flow of the mixed phase hydrogenation reactor, reduces feeding quantity of the front depropanizing tower, energy consumption and equipment investment, and is propitious to improve selectivity.
Owner:CHINA PETROLEUM & CHEM CORP +1

Selective hydrogenation catalyst for carbon five fraction and preparation and use thereof

The invention provides a selective hydrogenation catalyst for C5 fraction. The catalyst takes a compound of alumina and molecular sieves as a carrier and takes metals in the IA or IIA group, the VIII group, the IVA group and the IB group as active components. The compound carrier is soaked in aqueous solution of metallic compound in the IA/IIA group and is soaked in water soluble salt solution of the metals in the VIII group, nitrate solution of the metals in the IVA group and nitrate solution of the metals in the IB group by one step or multiple steps; after being soaked by one step, the compound carrier is dried for 12-20h at the temperature of 80-200 DEG.C, and then is calcined for 1-12 hours at the temperature of 350-650 DEG C. When the selective hydrogenation is carried out on unsaturated compounds in the C5 fraction by the catalyst, the transformation ratio of alkyne hydrogenation is more than or equal to 45%, the transformation ratio of dialkene is 15-35%, the content of alpha position olefin after hydrogenation is more than or equal to 15% and can meet the need of producing alpha-resin with high quality in the process of subsequent production, thus improving the quality of the alpha-resin products.
Owner:SINOPEC LANZHOU GASOLINEEUM CHEM IND CORP
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