Capital and total cost targets for mass exchange networks - Part 2: Detailed capital cost models

被引:38
作者
Hallale, N
Fraser, DM [1 ]
机构
[1] Univ Cape Town, Dept Chem Engn, ZA-7700 Rondebosch, South Africa
[2] UMIST, Dept Proc Integrat, Manchester M60 1QD, Lancs, England
关键词
capital cost targets; pinch analysis; mass-exchange networks;
D O I
10.1016/S0098-1354(99)00318-X
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This part of the paper builds on the developments of Part 1. It starts by developing a targeting method for tray columns using detailed capital costing methods. The number of units, column diameters and tray spacings, and the distribution of units and trays will all be considered. The limitations of stages targeting are also discussed, leading to an;explanation of why stages targets may be beaten, and showing how continuous contactors are more analogous to heat exchangers than stagewise contactors. A procedure for determining capital cost targets for networks of continuous contactors (usually packed columns) is then developed. Networks featuring different exchanger specifications are also dealt with. As before, capital cost targets are combined with operating cost targets to give total annual cost targets. The design of networks to meet the targets is then discussed. Systems featuring significant differences in exchanger specifications may require some deviation from ideal (vertical) driving force use. The examples presented in this part of the paper demonstrate that the targets are accurate enough for preliminary design as well as pre-design optimisation. The work in both parts of this paper reduces the amount of design work required when evaluating processes at the conceptual stage. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1681 / 1699
页数:19
相关论文
共 22 条
  • [1] COST OPTIMUM HEAT-EXCHANGER NETWORKS .2. TARGETS AND DESIGN FOR DETAILED CAPITAL-COST MODELS
    AHMAD, S
    LINNHOFF, B
    SMITH, R
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1990, 14 (07) : 751 - 767
  • [2] AHMAD S, 1989, CHEM ENG RES DES, V67, P481
  • [3] AHMAD S, 1985, THESIS U MANCHESTER
  • [4] [Anonymous], 1984, ICHEME ANN RES M BAT
  • [5] Backhurst J. R., 1973, PROCESS PLANT DESIGN
  • [6] Coulson JM, 1993, CHEM ENG, V6
  • [7] Douglas J. M., 1988, Conceptual design of chemical processes
  • [8] El-Halwagi M., 1997, Pollution Prevention Through Process Integration: Systematic Design Tools
  • [9] SYNTHESIS OF MASS EXCHANGE NETWORKS
    EL-HALWAGI, MM
    MANOUSIOUTHAKIS, V
    [J]. AICHE JOURNAL, 1989, 35 (08) : 1233 - 1244
  • [10] Garrett DE, 1989, CHEM ENG EC