On a new MILP model for the planning of heat-exchanger network cleaning

被引:43
作者
Lavaja, JH [1 ]
Bagajewicz, MJ [1 ]
机构
[1] Univ Oklahoma, Sch Chem Engn, Norman, OK 73019 USA
关键词
D O I
10.1021/ie034178g
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a new mixed-integer linear model for the planning of heat-exchanger cleaning in chemical plants. The model maximizes the net present value based on the cost of cleaning and the cost of energy and takes into account changes in production rates and even changes in the properties and flows of the different streams throughout time. This is important for the case of petroleum distillation in refineries that process different types of crudes. The model is multiperiod and uses two different fouling models.
引用
收藏
页码:3924 / 3938
页数:15
相关论文
共 22 条
  • [1] ALLE A, 2003, IN PRESS COMPUT CHEM
  • [2] Barletta AF, 1998, HYDROCARB PROCESS, V77, P51
  • [3] Brooke A., 1998, GAMS USERS GUIDE
  • [4] CASADO E, 1990, HYDROCARB PROCESS, V69, P71
  • [5] COROMINAS J, 1993, COMPUT CHEM ENG, V17, P15
  • [6] Elahresh HA, 1999, PRES '99: 2ND CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, P269
  • [7] OPTIMUM EVAPORATOR CYCLES WITH SCALE FORMATION
    EPSTEIN, N
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1979, 57 (05) : 659 - 661
  • [8] Optimal cyclic cleaning scheduling in heat exchanger networks under fouling
    Georgiadis, MC
    Papageorgiou, LG
    Macchietto, S
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1999, 23 : S203 - S206
  • [9] Jain V, 1998, AICHE J, V44, P1623
  • [10] KERN DQ, 1998, PROCESS HEAT TRANSFE