当代化工
噹代化工
당대화공
CONTEMPORARY CHEMICAL INDUSTRY
2014年
7期
1333-1335
,共3页
催化裂化%汽油%干点
催化裂化%汽油%榦點
최화열화%기유%간점
FCC%Gasoline%End boiling point
国内某石化公司1 Mt/a 的催化裂化装置出现了重汽油干点偏高的情况。通过分析装置现有操作数据并针对该数据进行了详细核算,找到了导致重汽油干点偏高的具体原因。分析讨论了重汽油干点的影响因素,并提出了降低重汽油干点的调整方案。
國內某石化公司1 Mt/a 的催化裂化裝置齣現瞭重汽油榦點偏高的情況。通過分析裝置現有操作數據併針對該數據進行瞭詳細覈算,找到瞭導緻重汽油榦點偏高的具體原因。分析討論瞭重汽油榦點的影響因素,併提齣瞭降低重汽油榦點的調整方案。
국내모석화공사1 Mt/a 적최화열화장치출현료중기유간점편고적정황。통과분석장치현유조작수거병침대해수거진행료상세핵산,조도료도치중기유간점편고적구체원인。분석토론료중기유간점적영향인소,병제출료강저중기유간점적조정방안。
The heavy gasoline from 1 Mt/a FCC unit in a domestic petrochemical company has higher end boiling point. In this paper, through analyzing and calculating the existed operating data, specific reasons to cause higher end boiling point were determined. The influence factors of heavy gasoline end boiling point were discussed, and the solutions were put forward.