一种用于活化费托合成催化剂的多级卧式流化床反应器及连续活化工艺

By designing a multi-stage horizontal fluidized bed reactor, the problems of low efficiency and uneven activation quality in the Fischer-Tropsch synthesis catalyst activation process were solved, achieving efficient and uniform catalyst activation, thereby improving reaction efficiency and product quality.

CN119346009BActive Publication Date: 2026-07-17ZHEJIANG UNIV

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
ZHEJIANG UNIV
Filing Date
2024-10-18
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing Fischer-Tropsch synthesis catalyst activation technologies suffer from low processing efficiency in batch operations and uneven activation quality in continuous moving bed operations, which affect reaction efficiency and product quality.

Method used

A multi-stage horizontal fluidized bed reactor is adopted. Through the combined design of gas distribution plate, vertical baffle and flap valve, the continuous feeding and discharging of catalyst and uniform activation are achieved, reducing particle backmixing and improving activation efficiency.

Benefits of technology

This method achieves efficient and uniform catalyst activation, shortens the activation cycle, increases the throughput per unit time, and improves the activation quality and reaction efficiency of the catalyst.

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Abstract

本发明公开了一种用于活化费托合成催化剂的多级卧式流化床反应器及连续活化工艺。多级卧式流化床反应器主体为带圆弧的窄边卧式容器,沿反应器轴向布置2~4块气体分布板,将反应器分割成2~4级密相反应区;相邻反应区之间配有翻板阀作为催化剂通道;气体分布板下部配有活化气入口管,活化气经气体分布板连续鼓入反应区;粉体费托合成催化剂由催化剂进料槽连续加料,自上而下逐级流过多级反应区,催化剂与活化气发生还原反应活化。与普通流化床反应器相比,粉体费托合成催化剂在多级卧式流化床反应器内的连续流动可有效减少返混,停留时间分布更窄,使不同粒径催化剂活化质量更均匀,提高费托反应产品收率。
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