2013
DOI: 10.1093/ijlct/ctt033
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Organic Rankine cycles in waste heat recovery: a comparative study

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Cited by 25 publications
(19 citation statements)
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“…The model used is an extented version of a model used in previous work by the authors [17]. The model uses standard thermodynamic heat-balance relations are used to describe the components in the cycle: heat exchangers, pump and turbine.…”
Section: Orc Modelling Methodologymentioning
confidence: 99%
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“…The model used is an extented version of a model used in previous work by the authors [17]. The model uses standard thermodynamic heat-balance relations are used to describe the components in the cycle: heat exchangers, pump and turbine.…”
Section: Orc Modelling Methodologymentioning
confidence: 99%
“…The larger the UA value the larger the heat exchanger required. Specific power is 10 [17] defined as the power output divided by the mass flow rate of working fluid in the ORC.…”
Section: Orc Modelling Methodologymentioning
confidence: 99%
“…To understand the effect of changing heat inputs and sources in an organic Rankine cycle, Auld et al [54] introduced a method of pinch point analysis to model the ORC over a wide range of operating conditions using different working fluids for multiple heat sources. The heat sources were LP steam from an industrial plant utility system, hot brines from wells and waste heat available from internal combustion engines.…”
Section: Introductionmentioning
confidence: 99%
“…This can be used either to offset an industrial site's electricity demand or it may be fed into an electricity grid to generate a financial return. There is considerable interest in the organic Rankine cycle since this technology represents a flexible and relatively efficient means of generating a benefit from waste heat [5][6][7][8].…”
Section: Introductionmentioning
confidence: 99%
“…The choice of working fluid is influenced by many factors including toxicity, environmental impact in case of accidental release, stability, cost and thermodynamic properties over the range of temperatures and pressures experienced in the application. For some fluids, the temperature at which heat is input to the evaporation part of the cycle may be as low as 73.3 • C [6] while for others it may be as high as 340 • C [9]. Suitable working fluids for ORC include linear, branched and aromatic hydrocarbons, fluorinated hydrocarbons, siloxanes, ethers and alcohols.…”
Section: Introductionmentioning
confidence: 99%