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): doi: / Different fuels utilized in the industrial district firms Figure Legend:

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): doi: / Installed thermal power as a function of employees number Figure Legend:

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): doi: / Installed electric power as a function of employees number Figure Legend:

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): doi: / Power to thermal ratio as a function of installed electric power Figure Legend:

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): doi: / Simplified scheme of a cogenerative ORC plant Figure Legend:

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): doi: / T-S diagram of the ORC cycle with MDM Figure Legend:

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): doi: / ORC model flow sheet in Aspen Plus ® Figure Legend:

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): doi: / Heat transfer diagram for some of the considered working fluids Figure Legend:

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): doi: / Electric efficiency as a function of inlet thermal load, at various condensing pressures (kPa). Cogenerative operation. Figure Legend:

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): doi: / Electric efficiency as a function of inlet thermal load, at various condensing pressures (kPa). Non-cogenerative operation. Figure Legend:

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): doi: / Electricity to heat ratio as a function of inlet thermal load, at various condensing pressures (kPa). Cogenerative operation. Figure Legend:

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): doi: / Gross electric power as a function of inlet thermal load, at various condensing pressures (kPa). Non-cogenerative operation. Figure Legend:

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): doi: / Plant components allocation of exergy introduced with diathermic oil. Cogenerative operation, p CON = 14 kPa, Q in = 6000 kW. Figure Legend:

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): doi: / Plant components allocation of exergy introduced with diathermic oil. Non-cogenerative operation, p CON = 4 kPa, Q in = 6000 kW. Figure Legend: