Application Center - Maplesoft

Contact Maplesoft Request Quote

Application Center Applications Thermodynamic Calculations of Vapor Compression Refrigeration Cycle with Regeneration Preview

App Preview:

Thermodynamic Calculations of Vapor Compression Refrigeration Cycle with Regeneration

You can switch back to the summary page by clicking here.

Learn about Maple

Download Application

Thermodynamic Calculations of Vapor Compression Refrigeration Cycle with Regeneration

^{Author: Volodymyr voloshchuk}

^{Vl.volodya@gmail.com}

Introduction

There are a variety of ways that the refrigeration cycle can be tailored to suit an application in a better way (not always necessarily resulting in a higher COP) than the simple (basic) vapor compression cycle.

Addition of a single heat exchanger to the basic vapor compression cycle, exchanging heat between the fluid leaving the evaporator and the fluid leaving the condenser benefits of this cycle modification.
First, since the specific enthalpy remains constant during expansion, a reduction of the specific enthalpy prior to expansion results in a reduction of specific enthalpy prior to evaporation. Therefore the unit will have more evaporative heat transfer to provide more evaporator cooling capacity. Second, the state prior to compression is further away from the saturated vapor line. For most compressors, it is imperative
that the state of the refrigerant prior to compression does not have any liquid in the form of droplets or mist, since liquid entrained in a vapor undergoing compression tends to damage the fast moving parts of a compressor, seriously degrading the performance and working life span of the compressor. For this reason, it is usually desirable for the refrigerant to enter the compressor as a superheated vapor, several degrees above the saturation temperature at the pre-compression pressure. The internal heat exchanger, by increasing the enthalpy and temperature of the pre-compression refrigerant, assists in ensuring that a superheated vapor with no liquid droplets enters the compressor.

This application is for thermodynamic calculations of vapor compression refrigeration cycle with regeneration

Creation functions on properties and processes of working fluids

with(ThermophysicalData):

Vapor pressure on the saturated line as a function of temperature

Liquid pressure on the saturated line as a function of temperature

Liquid temperature on the saturated line as a function of pressure

Vapor temperature on the saturated line as a function of pressure

Liquid specific enthalpy on the saturated line as a function of temperature

Liquid specific enthalpy on the saturated line as a function of pressure

Vapor specific enthalpy on the saturated line as a function of pressure

Liquid specific entropy on the saturated line as a function of temperature

Liquid specific entropy on the saturated line as a function of pressure

Vapor specific entropy on the saturated line as a function of pressure

Temperature as a function of pressure and specific entropy

Temperature as a function of pressure and specific enthalpy

Specific enthalpy as a function of pressure and temperature

Specific entropy as a function of pressure and temperature

HCOMPRESSIONPTPEFFwf := proc (p1, T1, p2, eff, wf) local h1, s1, s2_is, T2_is, h2_is; h1 := HPTwf(p1, T1, wf); s1 := SPTwf(p1, T1, wf); s2_is := s1; T2_is := TPSwf(p2, s2_is, wf); h2_is := HPTwf(p2, T2_is, wf); return h1+(h2_is-h1)/eff end proc:

Input Data

Temperature of heat source fluid at evaporator outlet

(3.1)

Temperature of heat consumption fluid at condenser outlet

(3.2)

Temperature difference at the cold end of the evaporator

(3.3)

Temperature difference at the hot end of the condenser

(3.4)

Temperature difference at hot end of the regenerator

(3.5)

Isentropic efficiency of the compressor

(3.6)

Working fluid

(3.7)

Calculations

Temperature of the working fluid at the evaporator intlet

(4.1)

Pressure of the working fluid at the evaporator intlet

(4.2)

Pressure of the working fluid at the compressor outlet

(4.3)

Pressure of the working fluid at the condenser outlet

(4.4)

Temperature of the working fluid at the condenser outlet

(4.5)

Specific enthalpy of the working fluid at the condenser outlet

(4.6)

Specific entropy of the working fluid at the condenser outlet

(4.7)

Pressure of the working fluid at the compressor intlet

(4.8)

Temperature of the working fluid at the compressor intlet

(4.9)

Specific enthalpy of the working fluid at the compressor intlet

(4.10)

Specific entropy of the working fluid at the compressor intlet

(4.11)

Specific enthalpy of the working fluid at the compressor outlet

(4.12)

Enhtalpy change in the compressor after actual compression

(4.13)

Temperature of the working fluid at the compressor outlet

(4.14)

Specific entropy of the working fluid at the compressor outlet

(4.15)

Temperature of saturated liquid of the working fluid at the evaporator inlet

(4.16)

Specific enthalpy of saturated liquid of the working fluid at the evaporator inlet

(4.17)

Pressure of the working fluid at the compressor intlet

(4.18)

Temperature of saturated vapor of the working fluid at the evaporator outlet

(4.19)

Specific enthalpy of saturated vapor of the working fluid at the evaporator outlet

(4.20)

Specific enthalpy of the working fluid at the regenerator outlet

(4.21)

Pressure of the working fluid at the regenerator outlet

(4.22)

Temperature of the working fluid at the regenerator outlet

(4.23)

Specific entropy of the working fluid at the regenerator outlet

(4.24)

Specific enthalpy of the working fluid at the evaporator intlet

(4.25)

Quality of the working fluid at the evaporator intlet

x__5 := Units:-Standard:-`*`(Units:-Standard:-`+`(h[5], Units:-Standard:-`-`(`h__sl,5`)), Units:-Standard:-`/`(Units:-Standard:-`+`(h__6, Units:-Standard:-`-`(`h__sl,5`))))