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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

green house gases such as co2 and so2 . A study by American EPA has demonstrated that residential fossil fuel<br />

heating system is in the USA produced anywhere from 1.2 to 36 times the environmental co2emissions from<br />

15% to 77% could be avoided through the application <strong>of</strong> GHSP systems .<br />

3. Experimentation<br />

For a general steady state, steady flow process, the four balance equations, namely mass, energy, entropy and<br />

energy balance equations are applied to ground source heat pump (GSHP) in ordered to find the heat input, the<br />

rate <strong>of</strong> energy decreased, the energy and exergy efficiencies the mass and energy balance equations as well as the<br />

exergy destruction obtained using the entropy and exergy balance equation for each <strong>of</strong> GSHP componets are<br />

discussed in the following sections. Fig shows schematic diagram <strong>of</strong> GSHP considered for thermodynamic<br />

analysis. The GSHP system consists <strong>of</strong> compressor, condenser, expansion valve, evaporator, fan-coil unit and<br />

ground heat exchanger. It is assumed that the flow is steady through every component <strong>of</strong> the GSHP system heat<br />

loss is ignored the governing equation for the individual components <strong>of</strong> the systems are derived as follows :<br />

Compressor<br />

Using the notation used to represents various stage points in GSHP system; the mass balance equation for<br />

compressor can be expressed as<br />

1 =2 = r<br />

assuming no heat loss, using the energy balance equation the work input to the compressor can be expressed as<br />

comp = r (h2-h1)<br />

The exergy destruction, xdest,comp can be computed using exergy generation and energy balance equations .<br />

Using these equation an expression for xdest,comp is given as follows<br />

xdest,comp = r (Ψ1- Ψ2 ) + comp,act<br />

Energy for any component can be found out using the formulas:<br />

Exergy Ψ = (h-h0)-T0(s-s0)<br />

Condenser<br />

Mass balance for refrigerant flow in the condenser can be denoted as<br />

2 = 3 = r<br />

similarly the mass balance for air flow in the fan coil unit which is connected to the condenser for heat<br />

extraction, can be expressed as<br />

5 = 6 = w<br />

the energy balance for refrigerant and air sides are given by<br />

cond = r (h2-h3)<br />

cond= fc= w =Cw (T5-T6)<br />

The exergy destruction in the condenser is expressed as<br />

Èxdest,cond =r(Ψ2- Ψ3)+ w(Ψ6- Ψ5)<br />

127

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