炼油技术与工程 ›› 2022, Vol. 52 ›› Issue (10): 5-9.
• 工厂设计 • 上一篇 下一篇
张方方
收稿日期:
出版日期:
发布日期:
作者简介:
Zhang Fangfang
Received:
Online:
Published:
摘要:
以某厂1号、2号芳烃联合装置为例,综合分析了相隔十多年设计的两套装置在能耗及低温热利用方面的差别,以及2号芳烃的设计改进对装置能耗的影响。提高加热炉燃料热效率、优化精馏塔的操作条件,提高低温热利用效率等措施对降低装置能耗非常重要,2号芳烃的操作费用明显低于1号芳烃。特别是2号芳烃特有的蒸汽压缩系统将装置自产的低压蒸汽转化成次高压蒸汽,替代传统设计中的一些高压蒸汽用户,让热量利用更趋合理。随着热水制冷技术的逐步成熟,芳烃联合装置利用低温余热制取热水进而制冷的方案未来会有更大作为。
关键词: 芳烃联合装置, 能耗, 加热炉, 精馏塔顶冷凝热, 低温热
Abstract:
The article analyzes the difference in the energy consumption and low temperature heat recovery based on the 1# and 2# aromatics complex in a certain company. The effect of design improvement on the 2# aromatics complex is also discussed. Measures such as improving the thermal efficiency of heating furnace fuel, optimizing the operating conditions of rectification tower, and improving the low temperature heat utilization efficiency are very important to reduce the energy consumption of the unit. The operating cost of 2# aromatics complex is significantly lower than that of 1# aromatics complex. In particular, the unique steam compression system of 2# aromatics complex converts the low-pressure steam produced by the unit into sub high-pressure steam, replacing some high-pressure steam users in the traditional design, making the heat utilization more reasonable. With the development of hot water refrigeration technology, the aromatics complex will make greater achievements in the future by using low temperature waste heat to produce hot water and then refrigeration.
Key words: aromatics complex, energy consumption, heating furnace, condensation heat at the top of rectification tower, low temperature heat
张方方 . 大型芳烃联合装置能耗对比与设计改进[J]. 炼油技术与工程, 2022, 52(10): 5-9.
Zhang Fangfang . Energy consumption comparison and design improvement of large aromatics complex[J]. Petroleum Refinery Engineering, 2022, 52(10): 5-9.
0 / / 推荐
导出引用管理器 EndNote|Ris|BibTeX
链接本文: https://journal01.magtechjournal.com/lyjsygc/CN/
https://journal01.magtechjournal.com/lyjsygc/CN/Y2022/V52/I10/5
[1] 戴厚良.芳烃技术[M].北京:中国石化出版社,2014:1-28,435-439.
[2] 唐文,黄文章,石国峰,等.余热回收系统改造的节能降耗[J].石油化工设计,2017,34(1):38-39.
[3] 赵建伟.对二甲苯联合装置二甲苯加热炉综合改造分析[J].炼油技术与工程,2019,49(2):54-58.
[4] 杨旭东,董海芳.大型芳烃联合装置的优化设计[J].炼油技术与工程,2015,45(7):6-10.
[5] 张方方.大型芳烃联合装置在炼化一体化加工方案中的优化设计[J].石油炼制与化工,2021,52(3):99-104.
[6] 张树广,刘成军,柳泉润.压缩机蒸汽驱动方案对芳烃联合装置能耗的影响[J].石油炼制与化工,2020,51(2):110-114.