Published September 2013 | Version v1
Journal article

Optimal integration of organic Rankine cycles with industrial processes

  • 1. Chemical Engineering Department, Universidad Michoacana de San Nicolás de Hidalgo, Morelia, Mich. 58060 (Mexico)
  • 2. Chemical and Biological Sciences Department, Universidad Autónoma de Sinaloa, Culiacán, Sinaloa 80000 (Mexico)
  • 3. Adjunct Faculty at the Chemical and Materials Engineering Department, Faculty of Engineering, King Abdulaziz University, P.O. Box 80204, Jeddah 21589 (Saudi Arabia)
  • 4. Chemical Engineering Department, Texas A and M University, College Station, TX (United States)

Description

Highlights: • An optimization approach for heat integration is proposed. • A new general superstructure for heat integration is proposed. • Heat process streams are simultaneously integrated with an organic Rankine cycle. • Better results can be obtained respect to other previously reported methodologies. - Abstract: This paper presents a procedure for simultaneously handling the problem of optimal integration of regenerative organic Rankine cycles (ORCs) with overall processes. ORCs may allow the recovery of an important fraction of the low-temperature process excess heat (i.e., waste heat from industrial processes) in the form of mechanical energy. An integrated stagewise superstructure is proposed for representing the interconnections and interactions between the HEN and ORC for fixed data of process streams. Based on the integrated superstructure, the optimization problem is formulated as a mixed integer nonlinear programming problem to simultaneously account for the capital and operating costs including the revenue from the sale of the shaft power produced by the integrated system. The application of this method is illustrated with three example problems. Results show that the proposed procedure provides significantly better results than an earlier developed method for discovering optimal integrated systems using a sequential approach, due to the fact that it accounts simultaneously for the tradeoffs between the capital and operating costs as well as the sale of the produced energy. Also, the proposed method is an improvement over the previously reported methods for solving the synthesis problem of heat exchanger networks without the option of integration with an ORC (i.e., stand-alone heat exchanger networks)

Availability note (English)

Available from http://dx.doi.org/10.1016/j.enconman.2013.04.036

Additional details

Identifiers

DOI
10.1016/j.enconman.2013.04.036;
PII
S0196-8904(13)00233-1;

Publishing Information

Journal Title
Energy Conversion and Management
Journal Volume
73
Journal Page Range
p. 285-302
ISSN
0196-8904
CODEN
ECMADL

INIS

Country of Publication
United Kingdom
Country of Input or Organization
International Atomic Energy Agency (IAEA)
INIS RN
46001090
Subject category
S42: ENGINEERING;
Descriptors DEI
HEAT EXCHANGERS; MECHANICAL SHAFTS; OPERATING COST; OPTIMIZATION; POWER GENERATION; PROCESS HEAT; RANKINE CYCLE; WASTE HEAT
Descriptors DEC
COST; ENERGY; HEAT; MACHINE PARTS; THERMODYNAMIC CYCLES; WASTES

Optional Information

Copyright
Copyright (c) 2013 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.