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Emergy-based exergoeconomic and exergoenvironmental evaluation of a combined power and cooling system based on ORC-VCR

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Abstract

Ensuring efficient operation of energy conversion systems in terms of economics and ecology is a prime objective that should be addressed within the design, optimization, and development stages of such systems. Adopting appropriate measures for accurate assessment and comprehensive evaluation of thermodynamic systems is a sheer necessity for accomplishing this purpose. In this study, the newly developed emergy-based exergoeconomic (i.e., emergoeconomic) and emergy-based exergoenvironmental (i.e., emergoenvironmental) analyses have been employed to assess a combined power and cooling system, including a gas turbine cycle, a steam Rankine cycle, and an integrated organic Rankine cycle-vapor compression refrigeration (ORC-VCR) subsystem serving as a waste heat recovery unit. The merit of emergy-based methods is that they can evaluate and express results by an identical unit of measurement (i.e., sej) which enables us to undertake a fair and accurate comparison between the methods in question. The results showed that the combustion chamber, with the total economic emergy rate of 6.83E13 (sej h−1) and the total ecological emergy rate of 6.05E14 (sej h−1), was the most critical component in the entire system from both the economic and ecological viewpoints. Moreover, a parametric study was carried out on the entire system, as well as the ORC-VCR unit, to examine the effect of design parameters on the emergy-based monetary and ecological performances. Increasing the air compressor pressure ratio from 6 to 11 enhanced the entire system’s both emergy-based performances by almost 8%, followed by improvements made by the gas turbine isentropic efficiency and combustor inlet temperature, with 6.5% and 5.5%, respectively. However, other design parameters exerted limited impact. Regarding the ORC-VCR, raising the ORC turbine inlet temperature and the isentropic efficiencies associated with the ORC turbine and VCR compressor improved the emergy-based performances, while the reverse was observed for the ORC condenser and evaporator temperature rise.

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Abbreviations

\(\dot{E}_{{}}\) :

Exergy rate (kW)

\(f_{\text{m}}\) :

Emergoeconomic factor (%)

\(f_{\text{n}}\) :

Emergoenvironmental factor (%)

\(hy\) :

Operation hours per year (h year-1)

LS:

Lifespan (year)

LT:

Lifetime (h)

m :

Specific monetary emergy (sej GJ−1)

\(\dot{M}\) :

Monetary emergy rate (sej h−1)

M :

Component’s mass (kg)

n :

Specific ecological emergy (sej GJ−1º)

\(\dot{N}\) :

Ecological emergy rate (sej h−1)

\(\dot{Q}\) :

Heat transfer rate (kW)

r :

Relative emergy difference (%)

SEM:

Exergy-based specific emergy of a material (sej g-1)

\(\dot{U}\) :

Component-related monetary emergy rate (sej h-1)

\(\dot{V}\) :

Component-related ecological emergy rate (sej h-1)

\(\dot{W}\) :

Power (kW)

\(\dot{Z}\) :

Investment cost rate ($ h−1)

\(\beta\) :

Scale factor

\(\psi\) :

Emergy-based performance (%)

D:

Destruction

F:

Fuel

i:

Flow stream number

in:

Inlet

k:

Component number

M/m:

Monetary

N/n:

Ecological

net:

Net

out:

Outlet

P:

Product

Q:

Heat

system:

System

tot:

Total

W:

Work

CI:

Capital investment

CO:

Construction

DI:

Disposal

OM:

Operating and maintenance

AC:

Air compressor

APH:

Air preheater

CC:

Combustion chamber

EVA:

Evaporator

EXV:

Expansion valve

GT:

Gas turbine

GTC:

Gas turbine cycle

MC:

Mixing chamber

OC:

ORC condenser

OP:

ORC pump

ORC-VCR:

Organic Rankine cycle-vapor compression refrigeration

OT:

ORC turbine

SB:

Steam boiler

SC:

Steam condenser

SP:

Steam pump

SPECO:

Specific exergy costing

SRC:

Steam Rkine cycle

ST:

Steam turbine

VC:

VCR compressor

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Mahmoudan, A., Samadof, P., Kumar, R. et al. Emergy-based exergoeconomic and exergoenvironmental evaluation of a combined power and cooling system based on ORC-VCR. J Therm Anal Calorim 145, 1353–1372 (2021). https://doi.org/10.1007/s10973-020-10422-6

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