Victor Hugo Corrêa, Carlos Henrique Vassoler, Caliane Bastos Borba Costa, Mauro Antonio da Silva Sá Ravagnani and Leandro Vitor Pavão*,
{"title":"Optimization of Heat Integration Systems Considering Multiple Utilities, Organic Rankine Cycles, and Rigorous Thermodynamic Property Calculations","authors":"Victor Hugo Corrêa, Carlos Henrique Vassoler, Caliane Bastos Borba Costa, Mauro Antonio da Silva Sá Ravagnani and Leandro Vitor Pavão*, ","doi":"10.1021/acs.iecr.5c02120","DOIUrl":null,"url":null,"abstract":"<p >Energy integration is a widely studied subject in Process Synthesis. An interesting solution in heat integration is the coupling of heat recovery systems to Organic Rankine Cycles (ORCs). The relatively low operating temperature of these cycles enables heat recovery from low-temperature hot streams by conversion to electricity for revenue. However, the inclusion of ORC-related equations in Heat Exchanger Network (HEN) models increases the problem’s complexity. This study tackles the problem using an implicit heat integration method via a Pinch Operator with rigorous calculation of thermodynamic properties (enthalpy, entropy, etc.). Two case studies are approached here. In the first case study, efficiencies of approximately 14% were achieved for an <i>n</i>-pentane cycle. In the second case study, when isentropic pressure changes are considered, efficiencies for <i>n</i>-pentane, <i>n</i>-hexane, and <i>n</i>-perfluoro-pentane were found to be ca. 12%, 14%, and 10%, respectively. Additionally, the study includes detailed cost–benefit analyses for each condition in both case studies.</p>","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"64 34","pages":"16820–16832"},"PeriodicalIF":3.9000,"publicationDate":"2025-08-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.5c02120","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acs.iecr.5c02120","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Energy integration is a widely studied subject in Process Synthesis. An interesting solution in heat integration is the coupling of heat recovery systems to Organic Rankine Cycles (ORCs). The relatively low operating temperature of these cycles enables heat recovery from low-temperature hot streams by conversion to electricity for revenue. However, the inclusion of ORC-related equations in Heat Exchanger Network (HEN) models increases the problem’s complexity. This study tackles the problem using an implicit heat integration method via a Pinch Operator with rigorous calculation of thermodynamic properties (enthalpy, entropy, etc.). Two case studies are approached here. In the first case study, efficiencies of approximately 14% were achieved for an n-pentane cycle. In the second case study, when isentropic pressure changes are considered, efficiencies for n-pentane, n-hexane, and n-perfluoro-pentane were found to be ca. 12%, 14%, and 10%, respectively. Additionally, the study includes detailed cost–benefit analyses for each condition in both case studies.
期刊介绍:
ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.