Abstract

The organic Rankine cycle (ORC) is a popular and promising technology that has been widely studied and adopted in renewable and sustainable energy utilization and low-grade waste heat recovery. The use of zeotropic mixtures in ORC has been attracting more and more attention because of the possibility to match the temperature profile of the heat source by non-isothermal phase change, which reduces the irreversibility in the evaporator and the condenser. The selection of working fluid and expander is strongly interconnected. As a novel expander, a single screw expander was selected and used in this paper for efficient utilization of the wet zeotropic mixtures listed in REFPROP 9.1 in a low-temperature subcritical ORC system. Five indicators, namely net work, thermal efficiency, heat exchange load of condenser, temperature glide in evaporator, and temperature glide in condenser, were used to analyze the performance of an ORC system with wet and isentropic zeotropic mixtures as working fluids. The calculation and analysis results indicate that R441A with an expander outlet temperature of 320 K may be the suitable zeotropic mixture used for both open and close type heat source. R436B may be selected with an expander outlet temperature of 315 K. R432A may be selected with an expander outlet temperature from 295 K to 310 K.

Highlights

  • The characteristics of the world energy structure, which is dominated by fossil energy, have caused two long-term problems, namely, the depletion of fossil energy and the environmental pollution caused by the utilization of fossil energy

  • Organic substance is used as the working fluid of the organic Rankine cycle which is usually used for the exploitation and utilization of medium-low grade heat source

  • It can be seen that R441A, which is a wet zeotropic mixture, can be

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Summary

Introduction

The characteristics of the world energy structure, which is dominated by fossil energy, have caused two long-term problems, namely, the depletion of fossil energy and the environmental pollution caused by the utilization of fossil energy. They found the match condition with the heat source should be firstly satisfied when selecting working fluids. In order to make full use of the exergy in low-temperature heat source, selection of proper zeotropic mixture as working fluid is very important. This paper, in order efficiently to efficiently use the wet zeotropic mixture low-temperature subcritical a single screw expander selected and usedin inlow-temperature the systeminand for analysis. Zeotropicnamely mixturenet selection for using single expander conducted based onthis five indicators, work, thermal efficiency, heatscrew exchange load ofisOn condenser, glide inselection evaporator, and using temperature glide further calculation and analysis.

Basic Constraints and Preliminary Screening
Thermodynamic
Subcritical
Description and determination of state points in Figure
Results and Discussion
16 K to WhenTable the expander temperature varies glide fromin290
Thermodynamic Setting and Description
11. Relation
Conclusions
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