Catalyst continuous cyclic regeneration methane catalytic cracking hydrogen production device and hydrogen production system

By designing a continuous recycling device for catalysts, using water vapor to reorganize the regenerative catalyst, to solve the problem of no catalyst in the reactor after the catalyst is inactivated, realize the continuous recycling and high -efficiency hydrogenation of the catalyst, and avoid the safety of oxygen input safety. Hidden dangers.

CN119346011AActive Publication Date: 2025-01-24SHANGHAI PUDONG ENVIRONMENTAL DEV CO LTD +1

Patent Information

Application Number
CN202411471200.5
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-10-22
Publication Date
2025-01-24
Estimated Expiration
2044-10-22

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Abstract

The invention belongs to the technical field of methane catalytic cracking hydrogen production, and particularly relates to a catalyst continuous cyclic regeneration methane catalytic cracking hydrogen production device and a hydrogen production system. The hydrogen production device comprises a methane catalytic cracking reactor, a steam reforming regeneration reactor and a spiral conveyor, and the bottom of the methane catalytic cracking reactor is communicated with the steam reforming regeneration reactor through the spiral conveyor. A steam distributor is arranged in the steam reforming regeneration reactor, and the top of the steam reforming regeneration reactor is communicated with the top of the methane catalytic cracking reactor. Along with the catalytic cracking reaction, the deactivated catalyst settles to the bottom of the methane catalytic cracking reactor and is conveyed to the steam reforming regeneration reactor by the spiral conveyor, and steam upwards blown by the steam distributor is in contact with the deactivated catalyst, is regenerated and enters the catalytic cracking reactor again; a continuous cycle process of catalysis, inactivation, regeneration and catalysis is completed; the deactivated catalyst is regenerated through water vapor, so that potential safety hazards caused by oxygen entering are avoided.
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Citation Information

Patent Citations

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    CN104998654A

  • Alkane crystal lattice oxygen selectivity oxidized activating catalyze cracking catalyst and method of use thereof

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    CN107213854A

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