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Improving the fluid catalytic cracking unit in term of energy consumption, a simulation study

机译:模拟研究改进流化床催化裂化装置的能耗

摘要

Fluid catalytic cracking (FCC) process is a unit that converts heavy distillates like gas oil or residues to gasoline and middle distillates using cracking catalyst. Increased global focus on reducing energy consumption and emissions are working together to make FCC unit power recovery more attractive. The flue gas temperature from the FCC unit was about 700-750oC and it holds a lot amount of energy. The heat recovery steam generated (HRSG) was used to recover the heat of fluegas to generate a steam and electricity. Aspen HYSYS (version 7.0) software was used to calculate the energy that will be recovered. From the simulation, besides from the based case, four adjustment of the parameter was made which is the steam pressure requirement, flowrate of feedwater, outlet steam turbine pressure and the efficiency of the steam turbine. The result was obtained by all that adjustment as shown in Section 4.1. For the based case of this study, the required steam pressure, temperature and mass flow was 600psig, 500oC and 45000kg/hr meanwhile for the fluegas was 34psig, 715oC and 241800kg/hr. The electric power generated was 1.46MW. For the adjustment of parameters, it is to know the amount of the electricity at a difference condition. As a conclusion, the objective of this study was achieved by improving the FCC unit in term of energy recovery.
机译:流化催化裂化(FCC)工艺是使用裂化催化剂将重油(如粗柴油或残油)转化为汽油和中间馏分的装置。全球越来越关注减少能源消耗和排放,这使得FCC单位的电力回收更具吸引力。来自FCC装置的烟气温度约为700-750oC,它可容纳大量能量。产生的热量回收蒸汽(HRSG)用于回收烟气的热量,以产生蒸汽和电力。使用Aspen HYSYS(7.0版)软件来计算将要回收的能量。通过仿真,除了基于实例的情况外,还对参数进行了四个调整,分别是蒸汽压力要求,给水流量,蒸汽轮机出口压力和蒸汽轮机效率。如第4.1节所示,通过所有调整获得了结果。对于本研究的基础案例,所需的蒸汽压力,温度和质量流量分别为600psig,500oC和45000kg / hr,而对于烟道气则分别为34psig,715oC和241800kg / hr。产生的电力为1.46MW。为了调整参数,要知道在不同条件下的电量。综上所述,本研究的目的是通过改善FCC装置的能量回收率来实现的。

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