Extraction method of heavy fraction of ft synthetic product from slurry bed reactor

A Fischer-Tropsch synthesis and slurry bed technology, applied in chemical instruments and methods, hydrocarbon production from carbon oxides, chemical/physical processes, etc., can solve problems such as forced shutdown and excessive pressure drop of the device, and reduce the difficulty , low density, prolonging the effect of operating cycle

Active Publication Date: 2009-03-25
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

These finer particles will be taken out from the top of the slurry bed reactor by the gas phase flow and deposited in heat exchangers and other equipment, which will cause the entire device to be shut down due to excessive pressure drop in the gas circulation system.

Method used

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  • Extraction method of heavy fraction of ft synthetic product from slurry bed reactor
  • Extraction method of heavy fraction of ft synthetic product from slurry bed reactor

Examples

Experimental program
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Effect test

Embodiment 1

[0026] The Fischer-Tropsch synthesis Fe-Cu-K catalyst prepared by the method disclosed in US5324335 was used for testing. In the slurry phase of the slurry bed reactor, the concentration of the catalyst is 30wt%, the particle size distribution range is 40-200μm, and the production capacity of the heavy fraction of the Fischer-Tropsch synthesis product is 30 tons / hour.

[0027] Such as figure 2 As shown, the SL50*800 asymmetric metal sintered filter rod 1 produced by Beijing Antai Technology Co., Ltd. is installed in the slurry bed reactor used. A total of 40 groups of filter rods are arranged, and each group is composed of 10 parallel filter rods, and the filter rods are evenly arranged in the radial direction of the reactor. The filtration precision of the filter rod is 25 μm.

[0028] The device for fine filtration (secondary filtration) of the heavy fraction of the Fischer-Tropsch synthesis product is an automatic backwash filter system with a filtration precision of 0.2...

Embodiment 2

[0032] The Fischer-Tropsch synthesis Fe-based catalyst prepared by the method disclosed in CN1233463 was used for testing. In the slurry phase of the slurry bed reactor, the concentration of the catalyst is 30wt%, the particle size distribution range is 40-200μm, and the production capacity of the heavy fraction of the Fischer-Tropsch synthesis product is 30 tons / hour.

[0033] Such as figure 2 As shown, the SL50*800 asymmetric metal sintered filter rod 1 produced by Beijing Antai Technology Co., Ltd. is installed in the slurry bed reactor used. The filter rods are arranged in 35 groups, each group is composed of 10 parallel filter rods, and the filter rods are evenly arranged in the radial direction of the reactor. The filtration accuracy of the filter rod is 35 μm.

[0034] The device for performing fine filtration treatment (secondary filtration) on the heavy fraction of the Fischer-Tropsch synthesis product is an automatic backwash filter 2 with a filtration precision o...

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Abstract

The invention provides a method for extracting Fischer-Tropsch synthesis product heavy distillate from a slurry bed reactor, concretely comprising the following steps: in the slurry bed reactor, when a Fischer-Tropsch reaction gas phase stream and a slurry phase stream flow through a metal sintering filter stick arranged in a liquid phase of the slurry bed reactor, the Fischer-Tropsch synthesis heavy distillate and part of catalyst powder can be separated out from the slurry phase of the slurry bed reactor; and the Fischer-Tropsch synthesis heavy distillate and part of catalyst powder are fed into a subsequent solid-liquid separation device for further separating the Fischer-Tropsch synthesis heavy distillate and the catalyst powder, so as to make the obtained Fischer-Tropsch synthesis heavy distillate meet the demand of downstream processing. The method avoids the catalyst particles from being brought out from the top part of the reactor by the gas phase stream and depositing on equipment such as a heat exchanger after being further crushed, and also improves the operational stability of the slurry bed reactor and extends the operation cycle of the apparatus, and can also provide qualified Fischer-Tropsch synthesis product heavy distillate to downstream units.

Description

technical field [0001] The invention relates to a method for separating a slurry bed Fischer-Tropsch synthesis catalyst and a product heavy fraction. Background technique [0002] Fischer-Tropsch synthesis is an important indirect coal liquefaction technology for producing synthetic liquid fuels and chemical raw materials from coal. Due to the characteristics and technical and economic advantages of slurry bed Fischer-Tropsch synthesis, the technology of slurry bed Fischer-Tropsch synthesis has been vigorously developed in recent years. The slurry bed reactor requires that the particle size of the catalyst should not be too large, otherwise the catalyst and the product cannot form a slurry phase, but this also brings about the difficulty of separating the catalyst from the Fischer-Tropsch synthesis product. In order to solve this problem, people focus on the process of placing a filter device in the slurry bed reactor to extract the heavy fraction of the Fischer-Tropsch syn...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/00B01J8/22C07C1/04
Inventor 门卓武石玉林卜亿峰吕毅军王洪学
Owner CHNA ENERGY INVESTMENT CORP LTD
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