石油化工设计 ›› 2020, Vol. 37 ›› Issue (3): 12-15.doi: 10.3969/j.issn.1005-8168.2020.03.004

• 设备技术 • 上一篇    下一篇

烷基化装置脱异丁烷塔重沸器的设计

许步建   

  1. 中石油华东设计院有限公司,山东 青岛 266071
  • 收稿日期:2019-11-06 出版日期:2020-08-25 发布日期:2020-09-04
  • 作者简介:许步建,男,2013年毕业于天津大学化学工程专业,硕士,主要从事炼油设计工作,工程师。E-mail:xubujian@cnpccei.cn,电话:15266259371;0532-80950778

Design of Deisobutanizer Reboiler in Alkylation Unit

Xu Bujian   

  1. CNPC EastChina Design Institute Co., Ltd., Qingdao, Shandong, 266071
  • Received:2019-11-06 Online:2020-08-25 Published:2020-09-04

摘要:

脱异丁烷塔重沸器是烷基化装置的关键设备之一,通常为卧式热虹吸式重沸器。对于30t/a的烷基化装置来说,以导热油或低压蒸汽为热源的情况下,该重沸器壳体内径为1 500 mm左右。且随着装置规模的扩大,该重沸器尺寸会相应增大或多台重沸器并联使用,给设备管道设计、现场施工都带来了很大困难。在塔釜设置隔板,可有效地降低重沸器壳程进出口温度,提高重沸器传热温差。流程模拟结果显示: 塔釜设置隔板后,重沸器壳程进出口温度分别降低了24.3 ℃和23.6 ℃,同时塔顶、塔底产品的流量及规格保持不变。换热器计算结果显示:塔釜设置隔板后,对数平均温度差提高了47%,换热面积减少33%,选型后的壳体内径缩小了300 mm。另外,隔板的溢流作用也为重沸器进料提供了稳定的压头,大大地提高了塔底重沸系统的操作稳定性。对于烷基化装置反应流出物物系来说,由于进脱异丁烷塔前经过聚结分离脱除酸碱处理,设置隔板不存在重沸器堵塞问题。该方案无论对新建还是改造的烷基化装置来说,都不失为一种很好的优化工艺。

关键词: 烷基化 , 脱异丁烷塔 , 重沸器

Abstract:

Deisobutanizer reboiler is one of the key equipment in alkylation unit. It is usually horizontal thermosiphon reboiler. For a 300 kt/a alkylation unit, the inner diameter of the reboiler shell is approximately 1500mm under the condition that hot oil or low-pressure steam is the heat source. With the capacity expansion of the unit, the size of the reboiler will increase or several reboilers will be operated in parallel, which brings great difficulties to the piping design and field construction of equipment. Setting baffle in the column kettle can effectively reduce the inlet and outlet temperature of the reboiler shell side and improve the heat transfer temperature difference of the reboiler. The process simulation results show that after the baffle is set in the column kettle, the inlet and outlet temperature of the reboiler shell side decreases by 24.3℃ and 23.6℃ respectively, while the flow rates and specifications of the overhead and bottom products remain unchanged. The heat exchanger calculation results show that, after setting the baffle, the logarithmic average temperature difference increases by 47%, the heat exchange area decreases by 33%, and the inner diameter of the shell decreases by 300mm. In addition, the overflow of the baffle also provides a stable pressure head for the feed of the reboiler, which greatly improves the operational stability of the bottom reboiler system. For the effluent system of alkylation unit, there is no reboiler clogging problem in setting up the baffle due to the separation and removal of acid and alkali by coalescer before entering the deisobutanizer. This scheme can be regarded as a good optimization process for both new and modified alkylation units.

Key words: alkylation, deisobutanizer, reboiler