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.

CN224507042UActive Publication Date: 2026-07-17GUANGXI HESHENG NEW ENERGY EQUIPMENT CO LTD

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

Technical Problem

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.

Method used

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.

Benefits of technology

It improves gas-solid contact efficiency, simplifies catalyst replacement process, reduces downtime, lowers energy consumption, and enhances reaction uniformity and production efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

本实用新型提供了一种裂解气催化装置,包括:反应罐,所述反应罐的顶部设有入口,所述反应罐的底部设有出口;催化组件,所述催化组件设置于所述反应罐内,并均匀分布于流道上;供热组件,所述供热组件设置于所述反应罐内;利用旋流效应延长裂解气在反应罐内的流动路径,并通过限位卡槽与顶珠结构实现催化剂载板的快速拆装,显著提升了气固接触效率与催化剂更换便捷性,生产时可在不更换催化剂的前提下对催化剂进行再生,减少停工时间;结合折流板强化逆流换热,既能利用反应余热预热原料气,又可精准控制反应温度,避免催化剂局部烧结;该装置具有结构紧凑、传质高效、再生灵活及能耗低的特点,特别适用于中小型裂解气处理场景。
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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: ​