Abstract

In a recent review an optimal thermodynamics and associated new upper bounds have been proposed, but it was only relative to power delivered by engines. In fact, it appears that for systems and processes with more than one utility (mainly mechanical or electrical power), energy conservation (First Law) is limited for representing their efficiency. Consequently, exergy analysis combining the First and Second Law seems essential for optimization of systems or processes situated in their environment. For thermomechanical systems recent papers report on comparisons between energy and exergy analysis and corresponding optimization, but the proposed models mainly use heat transfer conductance modelling, except for internal combustion engine. Here we propose to reconsider direct and inverse configurations of Carnot machines, with two examples. The first example is concerned with “thermofrigo-pump” where the two utilities are hot and cold thermal exergies due to the difference in the temperature level compared to the ambient one. The second one is relative to a “combined heat and power” (CHP) system. In the two cases, the model is developed based on the Carnot approach, and use of the efficiency-NTU method to characterize the heat exchangers. Obtained results are original thermodynamics optima, that represent exergy upper bounds for these two cases. Extension of the proposed method to other systems and processes is examined, with added technical constraints or not.

Highlights

  • A cogeneration plant, called a Combined Heat and Power (CHP) production system, or “thermo-frigopump”, can operate at efficiencies greater than those achieved when heat and power are produced in separate or distinct processes

  • A new analytical approach based on the current models of the solid oxide fuel cell and gas turbine was elaborated [20], in which multiple irreversibilities existing in real hybrid systems are taken into account

  • A novel conceptualisation considering the steam cycle of a combined heat and power generator thermodynamically equivalent to a conventional steam cycle generator plus an additional virtual steam cycle heat pump [22] leads to the conclusion that the performance of CHP will tend to be significantly higher than that of real heat pumps operating at similar temperatures

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Summary

Introduction

A cogeneration plant, called a Combined Heat and Power (CHP) production system, or “thermo-frigopump”, can operate at efficiencies greater than those achieved when heat and power are produced in separate or distinct processes. First and Second Law analyses of gas engines, fuel cells or hybrid solar systems [1,5,6,7,11,14] have shown that the energy-saving effect increases with the system scale because the heat to power ratio of the system decreases [1], or that both the main energy and exergy loss take place at the parabolic trough collector [7], and that the polymer exchange membrane fuel cell (PEMFC)-based CHP system, operating at atmospheric pressure and low temperature, is the most efficient system when compared to a solid oxide fuel cell (SOFC) one [14]. The proposed thermodynamics approach perspective points out cold and heat cogeneration systems (CCHP), and extends to polygeneration systems [24,25] These concepts and methodologies could help better design, manage and integrate these systems in the future, with respect to environmental and economic concerns. The obtained results could differ due to the technical constraints considered

First Example
Thermo-Frigopump Thermodynamical Model
Efficiency Criterions Regarding Thermo-Frigopump
Application to Optimization of a Thermo-Frigopump
Case of the Energy Criterion
Case of the Exergy Criterion
Second Example
Efficiency Criterions Regarding CHP System
Some Results Concerning CHP System Exergetic Optimization
H C TSHi
Generalization
Conclusions
Full Text
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