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内构件结构对于二级环流反应器流动和传质影响规律研究OA

Research on the influence of internal structure on flow and mass transfer in a two-stage internal loop airlift reactor

中文摘要英文摘要

在二级环流反应器级间安装菱形内构件可有效抑制级间返混,促进气液两相传质.为进一步提高二级环流反应器的传质性能,对菱形内构件的结构参数进行优化.首先设计了 9 个具有不同结构参数的菱形内构件,然后对采用不同菱形内构件时环流反应器中的气泡流型、气含率以及体积氧传质系数进行了实验测量,分析了结构参数对气含率和体积氧传质系数的影响规律.实验结果表明,挡板宽度和菱形角度对第一级和第二级环流反应器有着重要影响.菱形角度为 45°时,各级气含率达到最大.表观气速为0.009 3~0.018 5 m/s、挡板宽度为17 mm 时的体积氧传质系数最高;而当表观气速提高到0.023 0~0.027 8 m/s、挡板宽度为 25 mm 时,体积氧传质系数最高.最后,建立了气含率和体积氧传质系数的经验关联式,可准确预测安装了菱形内构件的二级环流反应器的性能,为二级环流反应器的传质强化提供了可行方案,同时为环流反应器的理性设计提供了重要依据.

Installing diamond-shaped internals between the stages of a two-stage internal loop airlift reactor can effectively suppress inter-stage backmixing and enhance gas-liquid two-phase mass transfer.To further improve the mass transfer performance of the two-stage internal loop reactor,this study optimized the structural parameters of the diamond-shaped internals.First,nine diamond-shaped internals with different structural parameters were designed.Then,the bubble flow pattern,gas holdup,and volumetric oxygen mass transfer coefficient in the reactor with different diamond-shaped internals were measured experimentally.Based on the experimental data,the influence of structural parameters on gas holdup and volumetric oxygen mass transfer coefficient was analyzed.The experimental results show that baffle width and diamond angle have significant effects on both first and second stages of the reactor.When the diamond angle is 45°,the gas holdup in each stage reaches its maximum.At superficial gas velocity of 0.009 3~0.018 5 m/s,the volumetric oxygen mass transfer coefficient is the highest when the baffle width is 17 mm,while at superficial gas velocity of 0.023 0~0.027 8 m/s,it is the highest when the baffle width is 25 mm.Finally,empirical correlations for gas holdup and volumetric oxygen mass transfer coefficient were established,which can accurately predict the performance of the two-stage internal loop reactor with diamond-shaped internals,providing a feasible solution for mass transfer enhancement and an important basis for the rational design of internal loop airlift reactors.

胡玲;韩淑怡;邹鹏飞;宋文杰;高鑫;刘文亮;郭凯;张津;陈运强

中国石油工程建设有限公司西南分公司,四川 成都 610041中国石油工程建设有限公司西南分公司,四川 成都 610041中国石油工程建设有限公司西南分公司,四川 成都 610041天津大学化工学院,天津 300350中国石油工程建设有限公司西南分公司,四川 成都 610041中国石油工程建设有限公司西南分公司,四川 成都 610041天津大学化工学院,天津 300350||天津市催化科学与工程重点实验室,天津 300350中国石油工程建设有限公司西南分公司,四川 成都 610041中国石油工程建设有限公司西南分公司,四川 成都 610041

环流反应器气液两相流气液传质气泡群

Internal loop airlift reactorGas-liquid two-phase flowGas-liquid mass transferBubble swarm

《天然气与石油》 2026 (2)

32-43,12

中国石油集团工程股份有限公司科学研究与技术开发项目"超大型中高含硫天然气处理关键技术研究"(2023ZYGC-02-01)

10.3969/j.issn.1006-5539.2026.02.005

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