Enthalpy Table Algorithm for design of Heat Exchanger Network as optimal solution in Pinch technology

Abstract The Heat Process Integration with Pinch technology is divided into two separate parts – targeting with super-targeting and design of a solution. Super-targeting determines the minimal values for heat demand and minimal allowed temperature difference in heat exchangers. The second part is design of Heat Exchanger Network as applicable solution. A number of studies explore methods and techniques for design of Heat Exchanger Networks based on data from Pinch analysis. Some of them use different optimization methods and give complex solutions. This paper presents a modified technique for Heat Exchanger Network design. This technique uses a combination of Problem Table Algorithm (PTA) and Pinch Design Method (PDM). The main idea for this technique is the design of sub-networks of heat exchangers for every enthalpy interval determined by the breaking points on the hot and cold composite curves. All these sub-networks were connected into one Heat Exchanger Network in the same order as enthalpy intervals exist in composite curves' graphs. The created Heat Exchanger Network was simplified with the basic rules for network relaxing in Pinch technology. The results of this technique were Heat Exchanger Networks that have high-energy recovery, and it got the optimal solution, or it was close to it. This technique is easy to apply, but in some cases, the primary Heat Exchanger Network's designs could have a very complex composition.

[1]  J. W. Ponton,et al.  A fast method for the synthesis of optimal heat exchanger networks , 1974 .

[2]  Predrag Rašković,et al.  Process integration in bioprocess indystry: waste heat recovery in yeast and ethyl alcohol plant , 2010 .

[3]  Jiří Jaromír Klemeš,et al.  Forty years of Heat Integration: Pinch Analysis (PA) and Mathematical Programming (MP) , 2013 .

[4]  Peter Glavič,et al.  Integration of Flue Gas into the Process Flowsheet by Combined Pinch–MINLP Approach , 2002 .

[5]  Sharifah Rafidah Wan Alwi,et al.  STEP—A new graphical tool for simultaneous targeting and design of a heat exchanger network , 2010 .

[6]  Dechema chemistry data series. : Vapor-liquid equilibrium data collection. Vol. I, part 2d, Organic hydroxy compounds; Alcohols and Phenoles (Supplement 2). 790 pp., prepared by Gmelin , 1984 .

[7]  Frank Pettersson Heat exchanger network design using geometric mean temperature difference , 2008, Comput. Chem. Eng..

[8]  U. V. Shenoy,et al.  Heat Exchanger Network Synthesis:: Process Optimization by Energy and Resource Analysis , 1995 .

[9]  Ian C. Kemp,et al.  Pinch Analysis and Process Integration: A User Guide on Process Integration for the Efficient Use of Energy , 2007 .

[10]  Naoki Kimura,et al.  Improvement in Strategy for Design of Heat Exchanger Networks using Multiagent Framework , 2012 .

[11]  Truls Gundersen,et al.  Heat Integration: Targets and Heat Exchanger Network Design , 2013 .

[12]  B. Linnhoff,et al.  The pinch design method for heat exchanger networks , 1983 .

[13]  Bodo Linnhoff,et al.  A User guide on process integration for the efficient use of energy , 1994 .

[14]  Zainuddin Abdul Manan,et al.  SePTA - A new numerical tool for simultaneous targeting and design of heat exchanger networks , 2013, Comput. Chem. Eng..

[15]  X. X. Zhu Automated synthesis of HENs using block decomposition and heuristic rules , 1995 .