摘要
大连西太平洋石油化工有限公司常减压蒸馏装置在原设计能力为5Mt/a的基础上,通过对装置的换热流程、电脱盐、常压塔、减压塔、加热炉及余热回收系统的改造,使装置处理能力达到10Mt/a。改造后装置运行效果良好,主要技术参数均达到或优于设计指标,并开车一次成功。
The throughput of an atmospheric and vacuum distillation unit in Dalian West Pacific Petrochemical Company has been enlarged to 10 Mt/a from the original design capacity of 5 Mt/a by revamping. The revamping areas includ ed the heat exchange network, desalter, atmospheric distillation tower, vacuum d istillation tower; heater and surplus heat recovery system. Satisfactory results were achieved and main technical parameters were reached or better than the des ign indexes, and the start up was also success.
出处
《石油炼制与化工》
CAS
CSCD
北大核心
2005年第3期10-14,共5页
Petroleum Processing and Petrochemicals
