Heat exchanger network optimization

Gundersen, T. and Naess, L. (1988). The synthesis of cost optimal heat exchanger networks, an industrial review of the state of the art. Comput. Chem. Eng., 12(6), 503-530. 

Gunderson T and Naess L (1988) The Synthesis of Cost Optimal Heat Exchanger Networks An Industrial Review of the State of the Art, Comp Chem Eng, 12 503. 

Research on the synthesis of economically optimal heat exchanger networks (HENs) has been performed for over 15 years (Nishida et al., 1981). As a result of this research, two general conclusions have emerged (1) the optimum network generally features minimum or close to minimum utility consumption, and (2) the optimum network generally has a mini-... 

T. K. Pho and L. Lapidus. Topics in computer-aided design Part II. Synthesis of optimal heat exchanger networks by tree searching algorithms. AlChEJ., 19 1182,1973. 

Pho, T.K. and Lapidus, L., "Topics in Computer-Aided Design Part II. Synthesis of Optimal Heat Exchanger Networks by Tree Search Algorithms," AlChE Journal, Vol. 19, No. 6, pp 1182-1189, November 1973. 

Ponton, J.W. and Donaldson, R.A.B., "A Fast Method for the Synthesis of Optimal Heat Exchanger Networks," Chemical Engineering Science, Vol. 29, pp 2375-2377, 1974. 

Flowsheet analysis and HEN synthesis problem. A material balance has been completed for a process to manufacture styrene and an ethylbenzene byproduct from reactions involving methanol and toluene. See Figure 10.61 for a block flow diagram of the process with the results of material balance calculations. You are to develop an optimal heat exchanger network for this process. Note that ... 

The design of the heat exchanger network is greatly simplified if the design is initialized with an optimized value for... 

The overall inventory. In the preceding chapter, the optimization of reactor conversion was considered. As the conversion increased, the size (and cost) of the reactor increased, but that of separation, recycle, and heat exchanger network systems decreased. The same also tends to occur with the inventory of material in these systems. The inventory in the reactor increases with increasing conversion, but the inventory in the other systems decreases. Thus, in some processes, it is possible to optimize for minimum overall inventory. In the same way as reactor conversion can be varied to minimize the overall inventory, the recycle inert concentration also can be varied. 

Heat Exchanger Network Design Based on the Optimization of a Reducible Structure... 

The approach to heat exchanger network design discussed so far is based on the creation of an irreducible structure. No redundant features were included. Of course, when the network is optimized, some of the features might be removed by the optimization. The scope for the optimization to remove features results from the assumptions made during the creation of the initial structure. However, no attempt was made to deliberately include redundant features. 

Yee, T. F., and Grossmann, I. E., A Simultaneous Optimization Approach for the Synthesis of Heat Exchanger Networks, Paper 81d, Annual AIChE Meeting, Washington, 1988. 

Combinatorial. Combinatorial methods express the synthesis problem as a traditional optimization problem which can only be solved using powerful techniques that have been known for some time. These may use total network cost direcdy as an objective function but do not exploit the special characteristics of heat-exchange networks in obtaining a solution. Much of the early work in heat-exchange network synthesis was based on exhaustive search or combinatorial development of networks. This work has not proven useful because for only a typical ten-process-stream example problem the alternative sets of feasible matches are cal.55 x 10 without stream spHtting. 

Shenoy, U. V. (1995). Heat Exchange Network Synthesis Process Optimization by Energy and Resource Analysis. Gulf Phb. Co., Houston, TX. 

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