200万吨2f年催化裂化和重油加氢装置设计与生产的双向优化

《200万吨2f年催化裂化和重油加氢装置设计与生产的双向优化》由会员上传分享，免费在线阅读，更多相关内容在学术论文-天天文库。

1、ABSTRACTThesquarethroughonofSinopecAnqingBranch200tons/yearRFCCUand2milliontons/heavyoilhydrogenationunitinheavyoilprocessingroutetoexplorethedesignandproductionoptimization,putforwardthepointofviewofalargecatalyticNewArea,productionoptimizationgoodjobondownstreamproductionofheavyoilcata

2、lyticcrackingcatalyticoptimizationmeasurestoformarelativelycompleteoptimizationprocessforheavyoilprocessing,throughtheoptimizationofthebigcatalyticmaterials,reactionconditions,catalystlevelwithothermeasurestoimprovetheeconomicefficiencyofthewholeplant.Keywords:heavyoilcatalytic;crackingo

3、fheavyoilhydrogenation’optimizing’largecatalyticIII目录第一章绪论...........................................................1第二章催化裂化装置设计优化...........................................22.1核心装置工艺方案选择..............................................22.1.1催化裂化MIP-CGP（CleanGasoline&Propylene)工艺..........

4、........22.1.2反应器旋分器VQS与粗旋的方案比选................................52.2MIP工艺的设计优化................................................92.2.1外取热取热量设计优化............................................92.2.2MIP相关设备结构优化............................................10第三章重油加氢与重油催化裂化组合工艺设计优化..................

5、......123.1RICP组合工艺简介................................................123.2双向组合工艺的优势...............................................133.3双向组合工艺设计上的优化.........................................133.3.1低空速设计是最合理和最优化设计.................................143.3.2催化裂化主风量优化设计...........................

6、..............26第四章生产优化......................................................284.1建立“大催化”管理模式...........................................284.1.1大催化工艺概念.................................................284.1.2“大催化”在生产优化中的主要影响因素............................284.1.3生产优化原则.......................

7、............................294.2根据沿江原油特点，优化重油加氢装置地原料。.......................294.2.1原料性质变化...................................................294.2.2原油中钙含量高，采取脱钙措施...................................394.2.3从常减压开始，以催化为中心，优化好大催化的原料.................434.3操作优化...................