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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Different fuels utilized in the industrial district firms Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Installed thermal power as a function of employees number Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Installed electric power as a function of employees number Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Power to thermal ratio as a function of installed electric power Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Simplified scheme of a cogenerative ORC plant Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 T-S diagram of the ORC cycle with MDM Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 ORC model flow sheet in Aspen Plus ® Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Heat transfer diagram for some of the considered working fluids Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Electric efficiency as a function of inlet thermal load, at various condensing pressures (kPa). Cogenerative operation. Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Electric efficiency as a function of inlet thermal load, at various condensing pressures (kPa). Non-cogenerative operation. Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Electricity to heat ratio as a function of inlet thermal load, at various condensing pressures (kPa). Cogenerative operation. Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Gross electric power as a function of inlet thermal load, at various condensing pressures (kPa). Non-cogenerative operation. Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Plant components allocation of exergy introduced with diathermic oil. Cogenerative operation, p CON = 14 kPa, Q in = 6000 kW. Figure Legend:
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Date of download: 6/1/2016 Copyright © ASME. All rights reserved. From: Performance Analysis and Working Fluid Optimization of a Cogenerative Organic Rankine Cycle Plant J. Energy Resour. Technol. 2013;135(2):021601-021601-11. doi:10.1115/1.4023098 Plant components allocation of exergy introduced with diathermic oil. Non-cogenerative operation, p CON = 4 kPa, Q in = 6000 kW. Figure Legend:
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