裂解气催化装置
By extending the gas-solid contact path through the swirling effect and the limiting slot structure, and combining it with baffles to enhance countercurrent heat transfer, the problems of low mass transfer efficiency and difficult catalyst regeneration are solved, enabling rapid catalyst regeneration and temperature control, and improving the operational stability and economy of small and medium-sized cracking gas treatment units.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- GUANGXI HESHENG NEW ENERGY EQUIPMENT CO LTD
- Filing Date
- 2025-05-26
- Publication Date
- 2026-07-17
AI Technical Summary
Low mass transfer efficiency, difficulty in catalyst regeneration, and uneven temperature control are problems existing in current cracked gas catalytic cracking units, which affect operational stability and economy, especially in small and medium-scale production scenarios.
The gas-solid contact path is extended by using the swirling effect, and the catalyst carrier plate is quickly disassembled and assembled by using the limiting slot and top bead structure. Combined with the baffle plate to enhance countercurrent heat exchange, the catalyst can be regenerated online and the temperature is controlled.
It improves gas-solid contact efficiency, simplifies catalyst replacement process, reduces downtime, lowers energy consumption, and enhances reaction uniformity and production efficiency.
Smart Images

Figure CN224507042U_ABST
Abstract
Claims
1. A catalytic cracking gas plant characterized by: The utility model relates to a regeneration catalyst carrier plate and a regeneration catalyst carrier plate limiting slot, and the regeneration catalyst carrier plate limiting slot is arranged on the spiral flow guide plate of the catalyst assembly. The reaction tank is of a cylindrical structure, and a conical flow guide head is arranged at the top of the reaction tank. The regeneration catalyst carrier plate is a honeycomb ceramic carrier plate, and a regeneration catalyst layer is coated on the honeycomb ceramic carrier plate. The side of the limiting slot is provided with a top bead, the top bead is telescopically arranged in a sliding cavity through a spring, and the sliding cavity is opened in the side wall of the limiting slot. The catalyst assembly further comprises a regeneration gas input pipeline and a regeneration gas discharge pipeline, and the regeneration gas input pipeline and the regeneration gas discharge pipeline are communicated with the side wall of the reaction tank through valves.
2. The catalytic cracking device of the pyrolysis gas according to claim 1, characterized by: The heat supply assembly comprises a heating plate arranged on the side wall of the reaction tank, the lower part of the reaction tank is provided with an annular heat exchange channel, the annular heat exchange channel is circumscribed with a pyrolysis gas pipeline at the feed end, and the discharge end of the annular heat exchange channel is connected with the inlet.
3. The catalytic cracking device of the pyrolysis gas according to claim 1, characterized by: A baffle plate is arranged in the annular heat exchange channel.
4. The catalytic cracking device of the cracked gas according to claim 1, characterized by: 5. The catalytic cracking device of claim 1, wherein: 6. The catalytic cracking device of the cracked gas according to claim 1, characterized by: 7. The catalytic cracking device of claim 6, wherein: