Catalytic cracking device and method
By optimizing the gas-solid fluidization state and catalyst reuse in the multi-stage reaction unit and cracking reaction unit of the catalytic cracking device, the problems of low gas-solid mixing and contact efficiency and insufficient proportion of light hydrocarbon refining in the existing devices are solved, and efficient catalytic cracking and flexible product regulation are achieved.
Patent Information
- Application Number
- PCT/CN2023/130672
- Authority / Receiving Office
- WO · WO
- Patent Type
- Applications
- Current Assignee / Owner
- Priority Date
- 2023-09-20
- Filing Date
- 2023-11-09
- Publication Date
- 2025-03-27
AI Technical Summary
During the cracking process of heavy oil and light hydrocarbons, the gas-solid mixing and contact efficiency of existing catalytic cracking devices is low, resulting in difficult to flexibly regulate the product properties and distribution, and the proportion of light hydrocarbon refining is insufficient.
The multi-stage reaction unit and the cracking reaction unit are arranged in parallel. By setting an internal conveying pipe in the multi-variable diameter lifting pipe of the multi-stage reaction unit, the gas-solid fluidization state is optimized; a turbulent reaction section is set in the cracking settler of the cracking reaction unit to achieve efficient contact reaction between the light hydrocarbons and the catalyst, and the catalyst after cracking the light hydrocarbons is reused to the heavy oil reactor.
The gas-solid mixing and contact efficiency during the cracking of heavy oil and light hydrocarbons is improved, the catalytic reaction efficiency is enhanced, the tight coupling between heavy oil and light hydrocarbon reactor is achieved, the flexibility of regulating product properties and distribution is improved, and the refining ratio of light hydrocarbons is improved.