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Fe-Mn-based catalyst for preparing low-carbon olefin directly from synthesis gas and preparation method of Fe-Mn-based catalyst

A technology for low-carbon olefins and catalysts, which is applied in the field of Fe-Mn catalysts and their preparation, and can solve the problems of easy overheating, difficulty in removing heat from the reaction, and low weight selectivity of low-carbon olefins

Active Publication Date: 2017-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] One of the technical problems to be solved by this invention is that the Fischer-Tropsch synthesis reaction exists in the prior art because the Fischer-Tropsch synthesis reaction is a strong exothermic reaction. The problem of low weight selectivity, providing a new iron-based catalyst for direct synthesis of low-carbon olefins from synthesis gas

Method used

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  • Fe-Mn-based catalyst for preparing low-carbon olefin directly from synthesis gas and preparation method of Fe-Mn-based catalyst
  • Fe-Mn-based catalyst for preparing low-carbon olefin directly from synthesis gas and preparation method of Fe-Mn-based catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0030] Take 606.03g of ferric nitrate nonahydrate and 0.44g of rhenium trichloride to dissolve in water to prepare a solution, and then the solution and 400g of 25% by weight concentrated ammonia water are flowed in parallel and centrifuged, and washed with deionized water three times to obtain fresh Mixed precipitation of ferric hydroxide and rhenium oxide I; 13.45g of 50% by weight manganese nitrate and a certain amount of water are added to make solution II, solution II and mixed precipitate I are mixed and peptized to obtain colloidal slurry III; 49.5 g 40% SiO by weight 2 The sol and 0.084g potassium hydroxide were added to the slurry III, mixed and beaten, then 0.098g 15% by weight dilute sulfuric acid was added, and the pH of the slurry was adjusted to 5 with ammonia water to obtain a sol-like dispersion that is uniform and will not be stored for a long time. Layered uniform slurry IV (solid content 45%), the slurry is spray-dried to form, the sprayer inlet temperature is...

Embodiment 2

[0033] Take 606.03g of ferric nitrate nonahydrate and 44.49g of osmium trichloride to dissolve in water to make a solution, then the solution is mixed with 400g of 25% by weight concentrated ammonia water and centrifuged, and washed with deionized water three times to obtain fresh Mixed precipitation of ferric hydroxide and osmium oxide I; Dissolve 1345g of 50% manganese nitrate in water to make solution II, mix and peptize solution II with mixed precipitate I to obtain colloidal slurry III; make 1016g weight content 25% Al 2 O 3 The sol and 20.47g of cesium nitrate were added to the slurry III, mixed and beaten, and then 19.6g of 15% by weight dilute phosphoric acid was added, and the pH of the slurry was adjusted to 1 with dilute nitric acid. The sol-like dispersion was uniformly dispersed and would not be separated after a long time The uniform slurry IV (solid content 15%) is spray-dried to form the slurry. The inlet temperature of the sprayer is 200°C and the outlet tempera...

Embodiment 3

[0036] Take 367.43g of ferric citrate and 3.52g of rhenium trichloride to dissolve in water to make a solution, and then the solution and 400g of 25% by weight concentrated ammonia water are flowed in parallel and centrifuged, and washed with deionized water three times to obtain fresh hydroxide Mixed precipitation of iron and rhenium oxide I; 26.90g of 50% by weight of manganese nitrate and a certain amount of water are added to make solution II, and solution I and mixed precipitate II are mixed and beaten to obtain colloidal slurry III; 435g weight content 40 % SiO 2 The sol and 4.8g sodium hydroxide were added to the slurry III, mixed and beaten, and then 0.294g of 15% by weight dilute sulfuric acid was added, and the pH of the slurry was adjusted to 3 with dilute ammonia to obtain a sol-like dispersion that is uniform and will not be stored for a long time. Layered uniform slurry IV (solid content 35%), spray dried the slurry, sprayer inlet temperature is 230 ℃, outlet tempe...

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Abstract

The invention relates to an Fe-Mn-based catalyst for preparing low-carbon olefin directly from synthesis gas and a preparation method of the Fe-Mn-based catalyst and mainly solves the problems in the prior art that Fischer-Tropsch synthesis reaction is strong exothermic reaction, so that when a static bed is used, heat removal is difficult and temperature runaway is easily caused in a reactor; the catalyst is easily inactivated; and the weight selectivity of the low-carbon olefin is low. The catalyst adopted in the invention comprises the following components in parts by weight: a) 10-70 parts of supporters which are at least one of Si or Al oxides; b) 30-90 parts of active components containing a composition with a chemical formula of Fe100MnaBbCcOx in atomic ratio, wherein B is one of Re or Os, and C is one of alkali metals, so that the above technical problems are well solved. The Fe-Mn-based catalyst is applied to industrial production of preparing low-carbon olefin directly from synthesis gas.

Description

Technical field [0001] The invention relates to an Fe-Mn series catalyst for directly preparing low-carbon olefins from synthesis gas and a preparation method thereof Background technique [0002] my country’s energy resources are characterized by rich coal, less gas, and oil shortage. Environmental pollution caused by direct coal combustion has also been paid more and more attention. Therefore, the development of the process of converting coal / natural gas into petroleum products through synthesis gas can not only reduce the energy dependence on foreign countries. , And it is of great significance to solve the environmental pollution caused by coal burning. [0003] Utilize synthesis gas (the main components are CO and H 2 ) The Fascher-Tropsch (Fascher-Tropsch) synthesis process of synthesizing hydrocarbons under the action of a catalyst is an important way for indirect liquefaction of coal and natural gas. This method was invented by German scientists Frans Fischer and Hans Trops...

Claims

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Application Information

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IPC IPC(8): B01J27/043B01J27/045B01J27/187C07C1/04C07C11/04C07C11/06C07C11/08
Inventor 庞颖聪陶跃武宋卫林李剑锋
Owner CHINA PETROLEUM & CHEM CORP