By-product steam combined axial flow gas-solid phase fixed bed catalyst chamber

A catalytic reactor and axial flow technology, applied in the direction of chemical instruments and methods, chemical/physical processes, etc., can solve the problems of complex heat exchange elements and reduced investment in reactors, and achieve easy control and adjustment, convenient loading and unloading, and temperature rise Restoring the easy effect

Active Publication Date: 2008-08-27
EAST CHINA UNIV OF SCI & TECH
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Problems solved by technology

The reactor is a water-cooled reactor, the catalyst is loaded in the shell side, and water flows in the heat exchange element; the heat exchange element is a plate heat exchanger; the reactor can use the original

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  • By-product steam combined axial flow gas-solid phase fixed bed catalyst chamber

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Embodiment Construction

[0027] Hereinafter, specific embodiments of the present invention will be given with reference to the drawings, but the present invention is not limited to the following embodiments.

[0028] A combined axial flow gas-solid phase fixed-bed catalytic reactor for by-product steam, comprising a cylinder body 15, an upper head 16, an adiabatic reaction section, a water cooling section in a tube and a lower head 14, and the upper head 16 is provided with A gas inlet 1 and a manhole 17 are provided, and a catalyst unloading port 11 and a gas outlet 12 are provided on the lower head 14 .

[0029] The inner diameter of the cylinder 15 is 3.8 meters, and the upper part is an adiabatic reaction section, which is provided with two adiabatic layers: a first adiabatic layer 2 and a second adiabatic layer 4, the first adiabatic layer 2 is arranged above the second adiabatic layer 4; After the first heat insulation layer 2, there is a raw material gas cooling system composed of the first coo...

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Abstract

A combined axial flow gas-solid phase fixed bed catalytic reactor capable of producing steam by product comprises a cylinder body, an upper end plate, an heat insulating reaction section, an in-pipe water cooling section, and a lower end plate. Two heat insulating layers are disposed on the heat reaction section; a material gas cold shocking device including a cold shocking distributor and a cold shocking pipe is disposed in the back of each heat insulating layer. A heat exchange medium manifold, an in-pipe water cooling section catalyst bed, heat exchange pipes, a heat exchange medium distribution pipe and a lower support plate are disposed in the in-pipe water cooling section. Cooling medium is filled in the heat exchange pipe. The catalyst is filled between the heat exchange pipes and has a filling height 50-95% of total height of the reactor catalyst layer. The reactor is specially design based on the characteristics of a reversible exothermic reaction, has the advantages of simple structure, convenient charge/discharge of catalyst; easy heating reduction of catalyst, simple temperature regulation of catalyst bed, recovery of high potential energy reaction heat and steam byproduct, and is suitable for large-scale chemical production.

Description

【Technical field】 [0001] The invention relates to the technical field of chemical reaction equipment, in particular to a combined axial flow gas-solid phase fixed-bed catalytic reactor for by-product steam. 【Background technique】 [0002] In reversible exothermic reactions such as methanol synthesis, ammonia synthesis, carbon monoxide conversion, hydrogenation of organic compounds, dimethyl ether synthesis, liquid fuel synthesis, and ethylene oxide synthesis, solid particle catalysts are used, and heat affects the reaction results. And the problem of catalyst recycling; in the large-scale industrial production process, it is necessary to apply fixed bed catalytic reactor. [0003] At present, the technologies relevant to the present invention mainly contain: [0004] (1) Linde reactor [0005] Compared with the shell-and-tube Lurgi reactor in Germany, when the catalyst is loaded in the Linde reactor, the catalyst is loaded between the tubes of the heat exchange tubes, and ...

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Application Information

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IPC IPC(8): B01J8/02
Inventor 应卫勇房鼎业张海涛马宏方蔡进
Owner EAST CHINA UNIV OF SCI & TECH
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