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过程工程学报 ›› 2023, Vol. 23 ›› Issue (3): 359-374.DOI: 10.12034/j.issn.1009-606X.222151

• 面向“双碳”目标的流程再造专栏 • 上一篇    下一篇

煤间接液化费托合成浆态床反应器的研究进展

张丽1*, 杨勇1, 高军虎1, 张煜1, 张丽丽1, 杨超2, 李永旺1
  

  1. 1. 中科合成油技术股份有限公司煤基清洁燃料国家能源研究中心, 北京 101407 2. 中国科学院过程工程研究所,中国科学院绿色过程与工程重点实验室,北京 100190
  • 收稿日期:2022-04-29 修回日期:2022-06-13 出版日期:2023-03-28 发布日期:2023-03-28
  • 通讯作者: 张丽 zhangli1@synfuelschina.com.cn
  • 作者简介:张丽,博士,高级工程师,化学工程专业,E-mail: zhangli1@synfuelschina.com.cn
  • 基金资助:
    煤炭清洁高效分级转化利用技术及工业示范;煤液化高效催化剂

Research advances of slurry bubble column for Fischer-Tropsch synthesis of indirect coal liquefaction technology

Li ZHANG1*,  Yong YANG1,  Junhu GAO1,  Yu ZHANG1,  Lili ZHANG1,  Chao YANG2,  Yongwang LI1   

  1. 1. National Energy Research Center for Coal-based Clean Fuels, Synfuels China Co., Ltd., Beijing 101407, China 2. CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
  • Received:2022-04-29 Revised:2022-06-13 Online:2023-03-28 Published:2023-03-28

摘要: :随着煤炭间接液化技术在百万吨级商业示范装置上的成功应用,作为其核心设备的费托合成浆态床反应器,涉及气液固三相湍流流动、传热传质及反应,其随反应器直径放大及内构件结构布局的变化而发生改变,进而影响反应器性能的多个复杂过程,导致在反应器设计、放大及操作优化上面临巨大挑战,科研及工业界仍然持续重视。本综述分析了影响浆态床反应器流体力学性能的主要因素,对浆态床反应器的流型、气含率、气泡行为、传热等研究进行了总结。介绍了浆态床反应器核心内构件的结构特点及发展状况,回顾了浆态床在费托合成反应过程中的工业应用历程,并展望了费托合成浆态床的研究趋势。

关键词: 费托合成, 浆态床, 流体力学, 内构件, 工业应用

Abstract: Coal-to-liquid (CTL) is one of the most promising way to efficiently convert coal into fuels and chemicals promoting the clean and efficient utilization of coal resources. With the successful application of indirect coal liquefaction technology in million-ton commercial demonstration plants, the Fischer-Tropsch synthesis slurry bubble column as its core equipment involves gas-liquid-solid three-phase turbulent flow, heat/mass transfer and reaction that change with the enlargement of the reactor diameter and the structural layout of internals, which in turn affects multiple complex processes of reactor performance, resulting in huge challenges in reactor design, scale-up and operation optimization due to lack of information on hydrodynamics with internals over a wide range of operating conditions of commercial interest. Scientific research and industry still continue to pay attention to it. This work gives a state-of-the-art review of the recent studies on the slurry bubble column for gas-to-liquid Fisher-Tropsch processes. It analyzes the main factors affecting the hydrodynamic performance of slurry bubble column, summaries the research on flow pattern, gas holdup, bubble behavior, and heat transfer, introduces the structural characteristics and development of the internals such as gas distributor, internal filtration, and heat exchanger. The effects of various operating variables, including pressure, temperature, gas velocity, catalyst concentration, and reactor geometry on the hydrodynamic and transport parameters as well as the performance of slurry bubble column are discussed. Unfortunately, little effort has been put on reviewing the experiments and simulations for examining the effect of internals on the performance and hydrodynamics of slurry bubble column for Fischer-Tropsch and significant efforts are still required. The research progresses from basic research to engineering technology of slurry bubble column in coal indirect liquefaction process are reviewed. Perspectives are given on the potential application and future research of slurry bubble column. Process intensification technology using internals to improve the performance and computational fluid dynamics will be the development direction in the future.

Key words: Fischer-Tropsch synthesis, slurry bubble column, hydrodynamics, internals, industrial application