石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (8): 71-76.

• 基础研究 • 上一篇    下一篇

基于分子管理的模拟移动床吸附分离石脑油中的正构烷烃

刘军涛,倪腾亚,刘纪昌,沈本贤   

  1. 华东理工大学化学工程联合国家重点实验室
  • 收稿日期:2014-01-20 修回日期:2014-03-20 出版日期:2014-08-12 发布日期:2014-07-22
  • 通讯作者: 刘纪昌 E-mail:liujc@ecust.edu.cn
  • 基金资助:

    国家自然科学基金资助项目

ADSORPTION SEPARATION OF NORMAL PARAFFINS FROM NAPHTHA BY SIMULATED MOVING BED BASED ON MOLECULE-SCALE MANAGEMENT

Jun-Tao JunLIU, ,Liu Ji-chang,Benxian Shen   

  • Received:2014-01-20 Revised:2014-03-20 Online:2014-08-12 Published:2014-07-22
  • Contact: Liu Ji-chang E-mail:liujc@ecust.edu.cn

摘要: 基于分子管理的理念,以5A分子筛为吸附剂,分离石脑油中的正构烷烃和非正构烃。考察了模拟移动床(SMB)中分子筛对正构烷烃的吸附分离规律以及循环比、分配比、脱附剂比等因素对分离效果的影响。在操作压力2.0 MPa、操作温度170 ℃、石脑油质量空速0.024 h-1、切换时间900 s的条件下,优化的模拟移动床操作条件为:循环比2.25、分配比3.00、脱附剂比4。对于正构烷烃质量分数为31.95%的石脑油,经SMB液相吸附分离后,脱附油中正构烷烃质量分数达到87.76%,吸余油中非正构烃质量分数达到97.83%。与石脑油原料相比,以脱附油作为裂解原料时的乙烯收率提高13.1百分点;吸余油研究法辛烷值提高19.2个单位,芳烃潜含量提高10.2百分点。

Abstract: Based on molecule-scale management, using 5A molecule sieve as adsorbent, a liquid-phase simulated moving bed (SMB) technology was used to separate normal paraffins from naphtha. The rules of separation process and effect of circulation ratio, distribution ratio and desorbent/naphtha flow ratio on the separation performance of SMB were investigated. Under 2.0 MPa, 170 ℃, LHSV of 0.024 h-1 and switching time of 900 s, the optimized operating conditions are:desorbent/naphtha ratio of 4, circulation ratio of 2.25 and distribution ratio of 3.00. For the feed naphtha with the normal paraffin content of 31.95%, the content of normal paraffins in desorption oil reaches 87.76%, and the content of non-normal paraffins in the raffinate is 97.83%. Compared with the naphtha feed, the ethylene yield increases by 13.1 percentage points using the desorption oil as a steam cracking feed; RON and the potential aromatics content of the raffinate increases by 19.2% and by 10.2 percentage points, respectively.