化工进展 ›› 2023, Vol. 42 ›› Issue (9): 4479-4495.DOI: 10.16085/j.issn.1000-6613.2022-1986
李春利1,2(), 韩晓光1, 刘加朋1,2(), 王亚涛3(), 王晨希1, 王洪海1,2, 彭胜3
收稿日期:
2022-10-25
修回日期:
2023-02-01
出版日期:
2023-09-15
发布日期:
2023-09-28
通讯作者:
刘加朋,王亚涛
作者简介:
李春利(1963—),男,博士,教授,研究方向为化工传递过程与设备。E-mail:lichunli_hebut@126.com。
基金资助:
LI Chunli1,2(), HAN Xiaoguang1, LIU Jiapeng1,2(), WANG Yatao3(), WANG Chenxi1, WANG Honghai1,2, PENG Sheng3
Received:
2022-10-25
Revised:
2023-02-01
Online:
2023-09-15
Published:
2023-09-28
Contact:
LIU Jiapeng, WANG Yatao
摘要:
填料塔作为化工单元操作过程中重要的汽液传质设备,因具有传质效率高、整塔压降低、能耗低等优点,已经成为精馏操作中的关键设备。液体分布器是填料塔中重要的塔内件,其结构形式直接关系到液相物料在塔内的分布情况,从而影响填料塔的分离效果。本文系统介绍了液体分布器的发展现状,从自然流分布、径向分布系数等方面详细总结了分布质量对填料塔分离效率的影响;深入分析了国内外关于各种结构类型的液体分布器的理论研究以及设计优化过程;并总结了不同液体分布器分布质量评价方法的适用场景。文章最后对液体分布器的发展进行了展望,为液体分布器的设计与优化提供了思路。
中图分类号:
李春利, 韩晓光, 刘加朋, 王亚涛, 王晨希, 王洪海, 彭胜. 填料塔液体分布器的研究进展[J]. 化工进展, 2023, 42(9): 4479-4495.
LI Chunli, HAN Xiaoguang, LIU Jiapeng, WANG Yatao, WANG Chenxi, WANG Honghai, PENG Sheng. Research progress of liquid distributors in packed columns[J]. Chemical Industry and Engineering Progress, 2023, 42(9): 4479-4495.
分类方式 | 类型 |
---|---|
推动力 | 压力式和重力式 |
用途 | 通用型和特殊用途型 |
出口方式 | 孔流、堰流和薄膜流 |
结构 | 管式、槽式和盘式 |
材质 | 不锈钢、聚四氟、聚乙烯、聚丙烯 |
表1 液体分布器分类
分类方式 | 类型 |
---|---|
推动力 | 压力式和重力式 |
用途 | 通用型和特殊用途型 |
出口方式 | 孔流、堰流和薄膜流 |
结构 | 管式、槽式和盘式 |
材质 | 不锈钢、聚四氟、聚乙烯、聚丙烯 |
液体分布器 | 推动力 | 流出 方式 | 塔径 /m | 堵塞 可能性 | 气体 阻力 | 水平度 影响 | 腐蚀 影响 | 液面波动 倾向 | 雾沫 夹带 | 操作 弹性 | 喷淋密度范围 /m3·h-1·m-2 | 重量 | 分布 质量 |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
排管式 | 重力 | 孔流 | >0.45 | 大 | 小 | 液位低时大 | 大 | 无 | 否 | 中 | 2.5~75 | 中 | 高 |
排管式 | 压力 | 孔流 | >0.45 | 中 | 小 | 小 | 大 | 无 | 是 | 小 | 2.5~25 | 轻 | 中 |
孔盘式 | 重力 | 孔流 | <1.2 | 大 | 大 | 液位低时大 | 大 | 有 | 否 | 中 | 2.5~75 | 中 | 高 |
槽盘式 | 重力 | 孔流 | >1.2 | 大 | 中 | 液位低时大 | 大 | 有 | 否 | 小 | 3.7~170 | 中 | 高 |
槽式 | 重力 | 堰流 | >0.6 | 小 | 小 | 大 | 小 | 有 | 否 | 大 | 2.5~125 | 中 | 高 |
表2 5种液体分布器性能比较[4]
液体分布器 | 推动力 | 流出 方式 | 塔径 /m | 堵塞 可能性 | 气体 阻力 | 水平度 影响 | 腐蚀 影响 | 液面波动 倾向 | 雾沫 夹带 | 操作 弹性 | 喷淋密度范围 /m3·h-1·m-2 | 重量 | 分布 质量 |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
排管式 | 重力 | 孔流 | >0.45 | 大 | 小 | 液位低时大 | 大 | 无 | 否 | 中 | 2.5~75 | 中 | 高 |
排管式 | 压力 | 孔流 | >0.45 | 中 | 小 | 小 | 大 | 无 | 是 | 小 | 2.5~25 | 轻 | 中 |
孔盘式 | 重力 | 孔流 | <1.2 | 大 | 大 | 液位低时大 | 大 | 有 | 否 | 中 | 2.5~75 | 中 | 高 |
槽盘式 | 重力 | 孔流 | >1.2 | 大 | 中 | 液位低时大 | 大 | 有 | 否 | 小 | 3.7~170 | 中 | 高 |
槽式 | 重力 | 堰流 | >0.6 | 小 | 小 | 大 | 小 | 有 | 否 | 大 | 2.5~125 | 中 | 高 |
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