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Slurry bed reactor and reaction method

A technology of slurry bed and reactor, which is applied in the field of slurry bed reactor and reaction, can solve the problems of low gas-liquid contact area, catalyst deposition, large flow dead zone, etc. control and high response efficiency

Active Publication Date: 2021-07-30
SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In view of the above-mentioned shortcoming of prior art, the object of the present invention is to provide a kind of slurry bed reactor and reaction method, be used to solve the low gas-liquid contact area that single size bubble causes in the slurry bed reactor of prior art , serious back mixing, large flow dead zone, catalyst deposition and other problems

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  • Slurry bed reactor and reaction method
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  • Slurry bed reactor and reaction method

Examples

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Effect test

Embodiment 1

[0074] This embodiment provides a lap bed reactor, such as figure 1 As shown, including:

[0075] Reactor housing 102 for accommodating the paste bed 101;

[0076] A multi-stage fractal gas distributor 103 for distributing the reactant gas into a multi-scale reactant bubble, the multi-stage fracture gas distributor 103 is immersed in the lamination bed 101;

[0077] The heat exchange tube 104 for heat exchange with the reactants and maintains a preset temperature during the reaction, the heat transfer tube 104 is immersed in the slurry bed 101.

[0078] As an example, such as figure 1 As shown, the slurry bed reactor includes at least: reactor housing 102, multi-stage fractal gas distributor 103, and heat transfer tube 104. The reactor housing 102 is used to accommodate the lap bed 101, the multi-level fractal gas distributor 103, and the heat transfer tube 104 immersed in the slurry bed 101. Specifically, in the present embodiment, the slurry bed reactor is a vertically placed ca...

Embodiment 2

[0090] This embodiment provides a reaction method of a lap bed reactor, such as Figure 9 As shown, including the following steps:

[0091] 1) Provide a slurry bed reactor containing a slurry bed that further comprises a multi-stage fractal gas distributor and a heat transfer tube immersed in the slurry bed;

[0092] 2) Support the reactant gas to the multi-stage fracture gas distributor, and distribute the reactant gas into micron-stage bubbles and millimeters air bubbles by the multi-stage fracture gas distributor;

[0093] 3) Make the micron-stage bubble and the millimeter bubble pass through the restrictive heat pipe where the micrometer bubble and the millimeter bubble are thermally exchanged and reactive to form a product gas.

[0094] In step 1), see Figure 9 S1 step and figure 1 There is provided a lap bed reactor containing a slurry bed 101, and the slurry bed reactor further comprises a multi-stage fractal gas distributor 103 and a heat exchange tube 104 that is immersed ...

Embodiment 3

[0099] In this example, the reaction method of the pulp bed reactor and the second embodiment of the second embodiment will be described in the reaction method of the pulley bed reactor.

[0100] In the present embodiment, the reactor housing of the gas bed reactor is 2 meters, an axial height of 35 meters, and a gas-liquid solid separation device is provided with a gas-liquid solid separation device, a heat transfer tube. Heating medium circulation pipeline Figure 7 The "four-leaf" type bionic geometry is provided with a multi-stage fractal gas distributor at the bottom of the paste bed reactor.

[0101] Before the start of the reaction, a slurry bed is pre-provided in the reactor housing, and the liquid surface of the slurry bed is located 15 meters above the multi-stage fractal gas distributor, and the slurry bed is liquid. Paraffin as a solvent, the catalyst is a cobalt-based catalyst, and the mass fraction of the catalyst is 5%.

[0102] During the reaction, the reactant gas ...

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Abstract

The invention provides a slurry bed reactor and a reaction method. The slurry bed reactor includes: a reactor shell for containing the slurry bed; A fractional gas distributor, the multi-stage fractal gas distributor is submerged in the slurry bed; a heat exchange tube for heat exchange with reactants and maintaining a preset temperature during the reaction process, the heat exchange The tube is submerged in the slurry bed. The invention introduces a multi-stage fractal gas distributor to generate multi-scale bubbles for three-phase reaction, and overcomes the problems of low gas-liquid contact area, large flow dead zone, and catalyst deposition caused by single-size bubbles. In addition, the back-mixing phenomenon of bubbles is avoided by introducing heat exchange tubes with fractal structure, and a new three-phase slurry bed reactor with controllable flow and high reaction efficiency is obtained.

Description

Technical field [0001] The present invention relates to the field of chemical equipment devices, and more particularly to a lap bed reactor and reaction method. Background technique [0002] In the field of chemical industry, bioengineering, gas-liquid-solid three-phase react system is a very important system, typically use a bubble lap bed reactor, and the main components of their internal components include distributors, heat exchange tubes, and separation. Mero, etc., commonly used for biological fermentation, CO 2 A process of absorbing reaction, Fischer Tourism and methanol synthesis. [0003] Currently, the lap bed reactor for gas-liquid solid three-phase reactors generally exist problems with lower reaction efficiency due to single bubble size. For example, when the bubble size is between millimeters or cm, the larger bubble size will result in a reduction in gas-liquid contact area, reduce mass transfer reaction efficiency; relatively, when the bubble size is reduced to t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/22
Inventor 赵陆海波唐志永张亚恒彭词汪丹峰孙予罕
Owner SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI