摘要
阐述了中国石化扬子石化股份有限公司烯烃厂1#乙烯装置自产丙烷作为裂解原料掺入循环乙烷共裂解运行情况,分析了对裂解炉运行周期及分离系统操作的影响,并指出该举措给装置带来的经济效益。
The paper introduces the operation condition of co-cracking by adding propane which produced from 1 # Ethylene Plant of Yangzi Petrochemical Co, Ltd. to recycling ethane and analyses the factors that influence on the run length of cracking heater and operation of separation system. .
出处
《乙烯工业》
CAS
2003年第3期40-43,共4页
Ethylene Industry
