Fluidized bed catalyst for directly preparing low-carbon olefins from synthesis gas and producing method thereof

A technology of fluidized bed catalysts and low-carbon olefins, applied in the direction of physical/chemical process catalysts, metal/metal oxides/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem of low weight selectivity of low-carbon olefins, Catalyst is easy to deactivate, fixed bed reaction is difficult to remove heat, etc.

Active Publication Date: 2014-08-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems to be solved by the present invention is that in the existing technology of Fischer-Tropsch synthesis of low-carbon olefins, it is difficult to remove the heat of the reaction in the fixed bed, and it is easy to overheat, which makes the catalyst easy to deactivate, and the weight selectivity of low-carbon olefins is low. Provide A new fluidized bed catalyst for directly preparing low-carbon olefins from synthesis gas and a production method thereof, the production method uses low-carbon olefins (C 2 = -C 4 = ) as the first product, supplemented by other organic hydrocarbons

Method used

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  • Fluidized bed catalyst for directly preparing low-carbon olefins from synthesis gas and producing method thereof
  • Fluidized bed catalyst for directly preparing low-carbon olefins from synthesis gas and producing method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0029]Dissolve 606.03g of ferric nitrate nonahydrate and 0.88g of ammonium metavanadate in water to form solution I, dissolve 132.40g of ammonium heptamolybdate and 0.24g of scandium nitrate pentahydrate in water to obtain solution II, and mix solutions I and II Obtain solution III; dissolve 87.98g of zinc nitrate hexahydrate in water to make a solution, and flow it with 200g of ammonia water with a mass concentration of 6% (into the same container dropwise at a uniform rate according to the proportion of just complete reaction) to obtain zinc hydroxide precipitation , fully wash the precipitate with deionized water to obtain zinc hydroxide; add zinc hydroxide to solution Ⅲ and mix and beat to obtain slurry Ⅳ, dissolve 0.08g of potassium hydroxide in water to obtain solution Ⅴ and then add it to the slurry Mix and beat in IV to obtain slurry VI, then adjust the pH value of the slurry to 5 with ammonia water, obtain the required catalyst slurry (solid content 15wt%) after full s...

Embodiment 2

[0032] Dissolve 606.03g of ferric nitrate nonahydrate and 569.13g of titanium tetrachloride in water to form solution I, dissolve 3.64g of bismuth nitrate pentahydrate and 86.19g of yttrium nitrate hexahydrate in water to obtain solution II, and mix solutions I and II Obtain solution III; dissolve 932.86g of zirconium nitrate pentahydrate in water to make a solution, and flow it with 2500g of ammonia water with a mass concentration of 6% (into the same container dropwise at a uniform rate according to the proportion of just complete reaction) to obtain zirconium hydroxide Precipitate, fully wash the precipitate with deionized water to obtain zirconium hydroxide; add zirconium hydroxide to solution III, mix and beat to obtain slurry IV, dissolve 20.23g of cesium hydroxide in water to obtain solution V and then add it to the slurry Mix and beat material IV to obtain slurry VI, then adjust the pH value of the slurry to 1 with ammonia water, and obtain the required catalyst slurry ...

Embodiment 3

[0035] Dissolve 606.03g of ferric nitrate nonahydrate and 35.2g of ammonium metavanadate in water to form solution I, dissolve 218.40g of bismuth nitrate pentahydrate and 71.83g of yttrium nitrate hexahydrate in water to obtain solution II, and mix solutions I and II Obtain solution Ⅲ; take 960.2g of zirconium nitrate solution and flow it with 2580g of ammonia water with a mass concentration of 6% (into the same container dropwise at a uniform speed according to the proportion of just complete reaction) to obtain zirconium hydroxide precipitation, fully deionized water Wash the precipitate to obtain zirconium hydroxide; add zirconium hydroxide to solution III, mix and beat to obtain slurry IV, dissolve 6g of sodium hydroxide in water to obtain solution V, then add it to slurry IV, mix and beat to obtain slurry Ⅵ, adjust the pH value of the slurry to 3 with ammonia water, obtain the required catalyst slurry (solid content 35wt%) after full stirring, and spray the slurry to shape...

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Abstract

The invention relates to an iron-based fluidized bed catalyst for directly preparing low-carbon olefins from a synthesis gas and a producing method of the iron-based fluidized bed catalyst. The iron-based fluidized bed catalyst and the preparing method mainly solve the problems that in the existing low-carbon olefin Fischer-Tropsch synthesis technology, the reaction heat removal of a fixed bed is difficult, and the temperature runaway can easily occur, so catalysts can be easily inactivated, and the weight selectivity of the low-carbon olefins is low. Through the technical scheme that the iron-based fluidized bed catalyst comprises the following ingredients in parts by weight: (a) 10 to 70 parts of carriers: the carriers are selected from either zinc oxide or zirconium oxide; (b) 30 to 90 parts of active ingredients: the active ingredients comprise the following compounds with the chemical formula being Fe100AaBbCcOx according to the atomic ratio, wherein A is either V or Ti, B is either Mo or Bi, and C is alkali metal, the problems are perfectly solved. The iron-based fluidized bed catalyst and the preparing method can be used for industrial production of low-carbon olefin direct Fischer-Tropsch synthesis.

Description

technical field [0001] The invention relates to a fluidized bed catalyst used for directly preparing low-carbon olefins from synthesis gas and a production 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 ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/887B01J23/83B01J23/847C10G2/00
Inventor 庞颖聪陶跃武宋卫林李剑锋
Owner CHINA PETROLEUM & CHEM CORP
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