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Catalyst for directly preparing low-carbon olefin from microspherical synthesis gas, as well as preparation method thereof

A technology of low-carbon olefins and catalysts, which is applied in the field of catalysts and preparations for direct preparation of low-carbon olefins from microspherical syngas, which can solve the problems of wide product distribution and achieve reasonable particle size distribution, high specific surface area, uniform and stable distribution Effect

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is the uneven distribution of the catalyst in the process of preparing the iron-based catalyst by the co-precipitation method existing in the existing Fischer-Tropsch technology, first co-precipitation, then beating, and then drying and forming, which finally leads to the problem of low selectivity of low-carbon olefins. A new microspherical catalyst and its preparation method are provided. The catalyst prepared by this method is evenly distributed microscopically, and the microstructure of the final catalyst can be controlled by controlling the conditions in the preparation process to improve the previous co-precipitation method. The problem of wide distribution of products on the catalyst for the synthesis of organic hydrocarbons from the obtained synthesis gas has the advantage of high selectivity of low-carbon olefins

Method used

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  • Catalyst for directly preparing low-carbon olefin from microspherical synthesis gas, as well as preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] 1.96g of barium nitrate and 218.3g of cobalt nitrate hexahydrate were dissolved in water to make a solution, then the solution was precipitated in parallel with 450g of 6% by weight ammonia solution, the precipitate was filtered, and washed repeatedly with deionized water to obtain a fresh and clean solution. Mixed oxide I of barium oxide and cobalt oxide; take 606.03g of ferric nitrate nonahydrate dissolved in water to make solution II, take 0.084g of potassium hydroxide to make solution III; mix solution II and solution III and 49.3g weight 40% SiO 2 The sol was sequentially added to the mixed oxide I and stirred in a boiling water bath at 100°C. At the same time, the pH value of the slurry was adjusted to 5 with ammonia water, and peptized to obtain a sol IV with a solid content of 15% by weight. The sol was spray-dried and formed. The inlet temperature of the sprayer is 380°C, the outlet temperature is 230°C, and then roasted at a temperature of 750°C and roasted fo...

Embodiment 2

[0033] The copper nitrate trihydrate of 81.6g titanyl sulfate and 724.8g and the calcium nitrate tetrahydrate of 1.77g are dissolved in water and make solution, then this solution and the 20% by weight solution that contains the salt of wormwood of 560g co-current precipitation, will The precipitate was filtered and washed repeatedly with deionized water to obtain fresh and clean mixed oxide I of titanium oxide, copper oxide and calcium oxide; 606.03g of ferric nitrate nonahydrate was dissolved in water to form solution II, and 8.4g of hydrogen Potassium oxide was made into solution III; solution II and solution III were sequentially added to mixed oxide I and stirred in a water bath at 50°C, while dilute nitric acid was used to adjust the pH value of the slurry to 1, and peptized to obtain a solid content of 45% by weight The sol body IV, the sol is spray-dried and molded, the inlet temperature of the sprayer is 200°C, the outlet temperature is 100°C, and then roasted, the roa...

Embodiment 3

[0037] 813.6g of zirconium nitrate pentahydrate and 2.7g of 50% manganese nitrate and 38.5g of magnesium nitrate hexahydrate are dissolved in water to make a solution, and then the solution is cocurrently precipitated with a 20% by weight solution containing 530g of sodium carbonate, The precipitate was filtered and washed repeatedly with deionized water to obtain fresh and clean mixed oxide I of zirconia, manganese oxide and magnesium oxide; 606.03g of ferric nitrate nonahydrate was dissolved in water to form solution II, and 0.6g of Potassium hydroxide was made into solution III; solution II and solution III were sequentially added to mixed oxide I and stirred in an ice-water bath at 0°C. At the same time, the pH value of the slurry was adjusted to 4.5 with dilute ammonia water, and the solid content of 30 was obtained by peptization. % by weight of the sol body IV, the sol is spray-dried and molded, the inlet temperature of the spray machine is 280°C, the outlet temperature ...

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Abstract

The invention relates to a catalyst for directly preparing a low-carbon olefin from a microspherical synthesis gas, and is mainly used for solving the problems that the existing co-precipitation Fischer-Tropsch catalyst preparation technology comprises the following steps: firstly co-precipitating and then pulping and spray-forming, so that the slurry is substantially a non-homogenous body dispersed by adopting a physical method, the finial catalyst finished product is uneven and the hydrocarbon products on the catalyst are widely distributed. The problems are well solved by adopting the technical scheme that the preparation method comprises the following steps: firstly precipitating a part of components, then carrying out peptization on the obtained precipitates by using the salt solution of non-precipitated components to obtain chemically evenly dispersed sol, then spray-drying the sol, and then roasting at high temperature. The preparation method can be used for industrial production for a catalyst for synthesizing the low-carbon olefin from the synthesis gas. The catalyst is applicable to but not limited to such reactors as a fluidized bed and a slurry-state bed in which catalyst grains are required to be distributed according to the certain distribution rule.

Description

technical field [0001] The invention relates to a catalyst for directly preparing low-carbon olefins from microspherical synthesis gas and a preparation method thereof. Background technique [0002] With the rapid development of my country's economy, the demand for petroleum resources and its products is increasing day by day. my country's energy is characterized by rich coal, little gas, and oil shortage. Lack of oil resources and insufficient domestic oil supply have become a severe reality for my country's energy development. With the development of the national economy, the contradiction between oil supply and demand will continue to expand, and get rid of the energy structure. The dependence on oil resources has become an urgent problem to be solved. This has just prompted people to actively and diligently develop other alternative energy sources, and the environmental pollution caused by the direct combustion of coal has also been paid more and more attention. The dev...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/78B01J23/83B01J23/889B01J23/80C07C1/04C07C11/02C10G2/00
Inventor 庞颖聪陶跃武宋卫林李剑锋
Owner CHINA PETROLEUM & CHEM CORP
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