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Compressor Design General Equations If the suction pressure and the discharge pressures of the compressor are P s and P d respectively, then the specific work done by the compressor can be found using: w = P s v s ( k k 1 )(( P d P s ) ( k k1 ) 1 ) Here k is the index of compression. For the refrigerant R134a, it can be approximated to 1.15 under normal operating conditions. However, if more accuracy is required, k can be found from the equation: k = ln ( P s P d ) ln ( v d v s ) Based on the mass flow rate of the refrigerant, the compressor power consumption and the volumetric flow rate of refrigerant through the compressor can be found out sing: Pm× w ˙ V r m×v S Once we find the value of ˙ V r , the actual swept volume of the compressor can be found, if we know the volumetric efficiency of the compressor. The actual swept volume of the compressor is: ˙ V s = ˙ V r η v Assume a suitable stroke to bore ratio, θ based on the following guidelines: Vacuum pumps and high speed compressors: θ< 0.5 Fluorocarbon compressors: θ=0.8 Ammonia compressors: θ=1.0 High pressure compressors: θ=4.6 Once these values have been assumed, the bore of the cylinder can be found out using the equation: D= 3 240× ˙ V s π×θ× N Here N is the rotational speed of the compressor in rad / s . The general speed ranges for compressors are 1000 rpm to 1500 rpm . Once the bore of the cylinder is found, the length of stroke can be found using: L=θ× D The values of volumetric efficiencies for various compression ratios can be found using the following table (taken from Principles of Refrigeration, Dossat, R.J.)

Compressor Design

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Compressor Design for a refrigeration system. The compressor used is a reciprocating compressor.

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  • Compressor Design

    General Equations

    If the suction pressure and the discharge pressures of the compressor are Ps and Pd respectively,then the specific work done by the compressor can be found using:

    w=Ps v s(k

    k1)((

    PdPs

    )( kk1 )1)

    Here k is the index of compression. For the refrigerant R134a, it can be approximated to 1.15 undernormal operating conditions. However, if more accuracy is required, k can be found from theequation:

    k=ln(

    PsPd

    )

    ln(vdvs)

    Based on the mass flow rate of the refrigerant, the compressor power consumption and the volumetric flow rate of refrigerant through the compressor can be found out sing:

    P=mwV r=mv S

    Once we find the value of V r , the actual swept volume of the compressor can be found, if we knowthe volumetric efficiency of the compressor. The actual swept volume of the compressor is:

    V s=V rv

    Assume a suitable stroke to bore ratio, based on the following guidelines: Vacuum pumps and high speed compressors:

  • Calculations and Results

    The pressure drops at the suction and discharge valves have been assumed to be 0.2 bar and 0.4 bar respectively. Based on the properties of refrigerant at the exit of evaporator ( T e=8

    o C ) and at the entry of condenser ( T c=40

    o C ), the following following pressures have been found:P1=349.9kPa and P2=1017 kPa

    Hence the suction and the discharge pressures are:Ps=P120kPa=329.9kPa and Pd=P2+40 kPa=1057 kPa

    Further, the specific volumes at these states are:v s=0.06327m

    3/kg and vd=0.02032 m3/kg

    Based on these properties of refrigerant, the index of compression can be found out to be:

    k=ln (

    PsPd

    )

    ln(vdvs)=

    ln( 329.91057

    )

    ln ( 0.020320.06327

    )=1.025

    The specific work of the compressor is:

  • w=Ps v s(k

    k1)((

    PdPs

    )( kk1 )1)=329.9kPa0.02032m3 /kg( 1.025

    1.0251)(( 1057

    329.9)( 1.0251.0251

    )1)=24.65kJ /kg

    The actual power consumed by the compressor and the volumetric flow rate of the refrigerant are:P=mw=0.02361 kg/ s24.65kJ /kg=0.5821kW

    V r=mv s=0.02361 kg /s0.06327 m3/kg=0.001494 m3/s

    The compression ratio of the compressor is:

    rC=PdP s

    = 1057329.9

    =3.204

    For the above compression ration, the volumetric efficiency is estimated to be v=0.795 . Hence theswept volumetric flow rate of the refrigerant is:

    V s=V rv =

    0.0014940.795

    =0.001879 m3/s

    The refrigerant chosen here is R134a, which is a fluorocarbon refrigerant. Hence the stroke-to-boreratio, is assumed to be 0.8. The rotational speed of the compressor, N is taken to be

    1000 rpm which equals 104.7 rad /s .

    Hence the bore diameter of the compressor is:

    D= 3 240V sN = 3 2400.001879 m3/ s0.8104.7 =0.1109mHence the length of stroke is:

    L=D=0.80.1109=0.08868 m

    From the cycle analysis, the ideal work done by the compressor is:Pideal=m(h3h2)=0.02361 kg /s (281.5256.6)kJ /kg=0.5863kW

    Hence the efficiency of the compressor is:

    = PPideal

    =0.58210.5863

    =0.9832

    Critical parameters of the compressor:

    Bore diameter 110 mm

    Length of stroke 90mm

    Power consumed 0.6kW