摘要
介绍了中国石油化工股份有限公司洛阳分公司0.7 Mt/a连续重整装置使用国产连续重整成套技术进行改造的情况,对改造后装置出现的循环氢压缩机喘振、反应加热炉热负荷不足、催化剂循环提升不畅、不能低碳烧焦、催化剂再生系统氯腐蚀并跑损催化剂等问题进行了分析,并采取措施进行了优化和改进。整改优化后,国产先进技术的优势得到了发挥,装置实现了满负荷平稳运行的目标。
The existing 13 200 b/d catalytic reformer in SINOPEC Luoyang Company was revamped with domestic catalytic reforming process.The surge of recycle hydrogen compressor,insufficient heat duty of reactor heater,difficulty in catalyst circulation,failure in low-carbon coke burning,chloride corrosion in regenerator system and catalyst loss,etc after revamping were analyzed,and improvement and optimization measures were taken.After improvement and optimization,the technical advantages of domestic catalytic reformi...
出处
《炼油技术与工程》
CAS
2010年第5期46-49,共4页
Petroleum Refinery Engineering
关键词
连续重整
改造
优化
运行
continuous catalytic reforming
revamping
optimization
operation
