...
机译:适当馏分催化重质高产高产催化裂化油的研究
State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;
State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;
State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;
State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;
State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing, 102249, China;
E: void volume fraction of fluidized bed; ρ: gas density, gcm~(-3); ρ_b: catalyst bed density, g·cm~(-3); V_(ij): stoichometric coefficient for the reaction of lump i to lump j; k: rate constant of reaction, (kg·m~(-3))~(-1)·h~(-1); et al;
机译:重型石油焦油和重重催化 - 裂解煤气 - 油的焦化产品比较
机译:根据SARA分析数据的重油和催化转化产物的描述
机译:优化重油催化裂化(MIP)工艺中的产品分布
机译:中孔结构控制转化和产品在重型油催化裂化催化剂设计中的选择性
机译:催化蒸汽裂化工艺降低重油总酸值的评价
机译:通过催化裂化转化从菜籽油中实验室生产生物燃料和化学药品
机译:用催化剂组合氢气溶剂的组合裂解重油。 (第3部分)。催化活性对化学氢消耗的影响。
机译:玛雅瓦斯油和选定的加氢处理产物的催化裂解:局部报告