摘要
以低温甲醇洗无硫富甲醇闪蒸罐到CO2产品塔的两相流管线为例,按照SH/T 3035-2007规定的要求进行计算,通过与工程实践的对比,验证其计算的可行性。总结了低温甲醇洗装置中抑制两相流的三项措施。
In this paper the calculation of the gas-liquid two-phase line from V03 to CO2 product column in Rectisol unit is made in accordance with SH/T 3035-2007.The feasibility of such calculation in line with SH/T 3035-2007 is verified by comparison with the actual engineering design.Three proven measures to restrain two-phase flow in engineering design of Rectisol unit have been summarized.
出处
《化工设计》
CAS
2012年第1期3-5,1,共3页
Chemical Engineering Design
