烷基化装置 , 低温热水 , 节能改造 ," /> 烷基化装置 , 低温热水 , 节能改造 ,"/> alkylation unit,low temperature hot water,energy-saving revamping ,"/> <p class="MsoNormal" align="left" style="text-align:left;"> <b>某硫酸法烷基化装置的节能改造方案<span></span></b>

石油化工设计 ›› 2021, Vol. 38 ›› Issue (3): 64-67.doi: 10.3969/j.issn.1005-8168.2021.03.015

• 节能减排 • 上一篇    下一篇

某硫酸法烷基化装置的节能改造方案

王恩民   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2020-12-31 出版日期:2021-08-25 发布日期:2021-08-16
  • 作者简介:王恩民,男,2014年毕业于大连理工大学化学工艺专业,工学硕士,现主要从事石油化工设计工作。联系电话:010-84877793;

Energy-Saving Revamping Scheme for a Sulfuric Acid Alkylation Unit

Wang Enmin   

  1. SINOPEC Engineering Incorporation, Beijing, 100101
  • Received:2020-12-31 Online:2021-08-25 Published:2021-08-16

摘要:

生产烷基化油是炼油企业发展的必然趋势,然而该装置能耗相对较高,需要结合全厂供能条件进行优化。某炼厂建有一套30万t/a硫酸法烷基化装置,其能耗为135 kg(OE)/t烷基化油,同时该厂有大量的低温热水可以利用。基于此,设计了一个节能改造方案,通过最大化利用低温热水代替1.0 MPag(表)蒸汽,实现节约1.0 MPag(表)蒸汽27.0 t/h。通过本节能改造方案,该烷基化装置能耗降低约30.3 kgoe/t烷基化油。

关键词:

text-indent:0cm, 烷基化装置 ')">"> 烷基化装置 , 低温热水 , 节能改造

Abstract:

Alkylate production has become an inevitable trend for refineries. In consideration of the high energy consumption of alkylation unit, it’s necessary to optimize the operation of alky unit in combition with the energy supply conditions of the whole refinery. A refinery has a 300 kt/a sulfuric acid alkylation unit with 135 kgoe/t alkylate consumption, and a large amout of low-temperature hot water is available. An energy-saving revamping scheme is designed to save 1.0 MPag steam (27.0 t/h) by using low-termperature hot water as much as possible. The energy consumption of the unit can be reduced by 30.3 kgoe/t alkylate after the revamping.

Key words: alkylation unit')">

alkylation unit, low temperature hot water, energy-saving revamping