STEP-A new graphical tool for simultaneous targeting and design of a heat exchanger network

被引:74
作者
Alwi, Sharifah R. Wan [1 ]
Manan, Zainuddin A. [1 ]
机构
[1] Univ Teknol Malaysia, Proc Syst Engn Ctr PROSPECT, Skudai 81310, Johor, Malaysia
关键词
Pinch analysis; Stream Temperature versus Enthalpy Plot (STEP); Heat exchanger network (HEN) design; Targeting; Heat recovery; Maximum heat allocation (MHA); PINCH TECHNOLOGY; ENERGY TARGETS; GENERATION;
D O I
10.1016/j.cej.2010.05.009
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
For 40 years, composite curves (CCs) and grid diagram (G D) have been among the most popular graphical tools for designing optimal heat exchanger networks (HEN). However, since CCs represent the temperature versus enthalpy plot of composites rather than individual streams, they have some significant limitations. Among others, CCs cannot completely map individual hot and cold process streams, as well as process and utility streams, and cannot be used for HEN design. In addition, CCs cannot be conveniently and effectively used to predict minimum network area and the optimum Delta T(min) that should strictly be based on parameters and properties of individual as opposed to composite streams. Grid diagram on the other hand requires designers to provide or calculate stream temperatures as well as enthalpies, to do heat balance and to check temperature feasibility during HEN design as the diagram does not follow any temperature or enthalpy scale. This paper presents STEP (Stream Temperature vs. Enthalpy Plot) as a new graphical tool for simultaneous targeting and design of a HEN that overcomes the key limitations of CCs and the GD. The new STEPs are profiles of continuous individual hot and cold streams being mapped on a shifted temperature versus enthalpy diagram that simultaneously show the pinch points, energy targets and the maximum heat allocation (MHA). The MHA is graphically converted to an MER network and represented on a Heat Allocation and Targeting (HEAT) diagram in terms of STEP temperature and enthalpy. This paper also demonstrates that STEP can provide more realistic solutions for targeting multiple utilities and the minimum network area. STEP application on a palm oil refinery, and finally, its limitations, are also highlighted. With capabilities to overcome the limitations of CCs and GD. STEP can become a vital alternative graphical tool for optimal HEN design. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:106 / 121
页数:16
相关论文
共 23 条
[1]   COMMENTS ON IMPROVEMENTS ON A REPLACEMENT FOR THE LOGARITHMIC MEAN [J].
CHEN, JJJ .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (10) :2488-2489
[2]  
FLOWER JR, 1980, AICHE J, V25, P1
[3]  
Hohmann EC, 1971, THESIS U SO CALIFORN
[4]  
ITOH J, 1982, INT C PROC SYST ENG
[5]  
Kemp IC., 2007, Pinch analysis and process integration. A user guide on process integration for the efficient use of energy
[6]  
LIM FY, 2003, THESIS U TEKNOLOGI M
[7]  
*LINNH MARCH LTD, 1992, PROC INT 1A
[8]   SYNTHESIS OF HEAT-EXCHANGER NETWORKS .1. SYSTEMATIC GENERATION OF ENERGY OPTIMAL NETWORKS [J].
LINNHOFF, B ;
FLOWER, JR .
AICHE JOURNAL, 1978, 24 (04) :633-642
[9]   COST OPTIMUM HEAT-EXCHANGER NETWORKS .1. MINIMUM ENERGY AND CAPITAL USING SIMPLE-MODELS FOR CAPITAL COSTS [J].
LINNHOFF, B ;
AHMAD, S .
COMPUTERS & CHEMICAL ENGINEERING, 1990, 14 (07) :729-750
[10]  
LINNHOFF B, 1983, CHEM ENG RES DES, V61, P207