作者: Ligang Lin , Ying Kong , Jinrong Yang , Deqing Shi , Kekun Xie
DOI: 10.1016/J.MEMSCI.2007.03.052
关键词: Permeation 、 Fluid catalytic cracking 、 Engineering 、 Scientific method 、 Process simulation 、 Membrane 、 SCALE-UP 、 Petroleum engineering 、 Pervaporation 、 Gasoline 、 Process engineering
摘要: The significance and possibility of using pervaporation (PV) for deep desulphurization fluid catalytic cracking (FCC) gasoline have been widely recognized. aim this study was to build a bridge between experimental studies potential applications on pilot scale. Process simulation model developed. By applying the simulation, influence interstage heating manner process parameters, e.g., feed temperature, permeate pressure, sulfur content level retentate required membrane area rate investigated. Based results as well discussions considerable base data, scale-up plant designed established. It has demonstrated that can play an important role in optimizing during technology.