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Building Services Engineering 5th Edition Handbook

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152 Ventilation and air conditioning<br />

Large air-cooling plant comprises a multi-cylinder in-line or V-formation compressor, a shell<br />

and tube refrigerant to a water evaporator producing chilled water, and a shell and tube<br />

refrigerant to a water condenser where the refrigerant vapour is condensed into liquid and<br />

the heat given out is carried away by a water circuit to a cooling tower on the roof.<br />

2. The centrifugal compressor is used in large chilled-water plants where the noise and vibration<br />

produced by the reciprocating type would be unacceptable. A centrifugal impeller of small<br />

diameter is driven through a step-up gearbox from a three-phase electric motor. The lack of<br />

vibration and compactness of the very high-speed compressor makes siting the plant easier.<br />

3. The screw compressor has two meshed gears, which compress the refrigerant in the spaces<br />

between the helical screws. One gear is driven by an electric motor through a step-up<br />

gearbox. The compressor operates at high speed and has very low noise and vibration levels.<br />

The operation of a vapour-compression refrigeration plant is shown in Fig. 5.16.<br />

Refrigerants commonly used are non-toxic fluids with high latent heat. Refrigeration plant<br />

with a capacity of up to about 175 kW, and motor cars, uses refrigerant HFA134A (replaced<br />

R12, which is CCl 2 F 2 ), which boils at −29.8 ◦ C in the atmosphere. In a typical system it will be<br />

evaporated at 5 ◦ C under a pressure of 3.6 bar and condensed at 40 ◦ C at 9.6 bar. Larger plant<br />

uses fluorinated hydrocarbon R22 (CHClF 2 ), which has a greater refrigerating effect per kilogram<br />

but is more expensive.<br />

The coefficient of performance (COP) is an expression of cycle efficiency and is found from<br />

COP =<br />

heat absorbed by refrigerant in the evaporator W<br />

power consumption by the compressor W<br />

The vapour-compression cycle can be represented on a pressure–enthalpy diagram for the refrigerant<br />

as shown in Fig. 5.17. Referring to Figs 5.16 and 5.17, compression 1–2 raises the temperature<br />

of the refrigerant dry superheated vapour from about 20 ◦ Cto60 ◦ C, where it can then be cooled<br />

and condensed at a sufficiently high temperature to reject the excess heat from the building to<br />

the hot external environment.<br />

It condenses at 40 ◦ C and collects in the liquid receiver. This warm high-pressure liquid passes<br />

through an uninsulated pipe so that it is subcooled to below its saturation temperature (about<br />

20 ◦ C) at the expansion valve located alongside the evaporator.<br />

Low-temperature<br />

and pressure vapour<br />

Suction temperature<br />

sensing phial controls<br />

valve opening<br />

1 2<br />

Electric-motordriven<br />

compressor<br />

Superheated<br />

vapour<br />

Evaporator<br />

Condenser<br />

Refrigerant<br />

absorbs heat<br />

from the<br />

building<br />

Low-temperature<br />

liquid and some<br />

vapour at low<br />

pressure<br />

4 3<br />

Heat contained in<br />

refrigerant is<br />

rejected to the<br />

atmosphere<br />

Liquid receiver<br />

High-pressure warm liquid<br />

Thermostatic expansion valve<br />

5.16 Vapour-compression refrigeration system.

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