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2000 Hook-up Book - Spirax Sarco

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SYSTEM DESIGN<br />

62<br />

Compressed Air Systems<br />

Air Compressors<br />

Heat is released when air or any<br />

gas is compressed. The compressor<br />

must be cooled to avoid<br />

overheating, usually by circuating<br />

water through the jackets.<br />

Cooling is an important function<br />

which must be controlled to<br />

ensure maximum efficiency.<br />

Overcooling wastes water and<br />

leads to condensation within the<br />

cylinders, with deterioration of the<br />

lubricating oils. Undercooling<br />

reduces compressor capacity<br />

and can result in serious damage<br />

to the compressor. Automatic<br />

temperature control of cooling<br />

water flow ensures maximum efficiency.<br />

The atmosphere is a mixture<br />

of air and water vapor. Free air<br />

has a greater volume, and moisture<br />

holding capacity, than<br />

compressed air at the same temperature.<br />

As the compressed air<br />

is cooled after leaving the compressor,<br />

or between stages,<br />

some of the water is precipitated.<br />

This water must be drained from<br />

the system to avoid damage to<br />

pneumatic valves and tools.<br />

Choice Of Drainer Trap<br />

The quantities of water which<br />

must be drained from the air are<br />

relatively small, even on quite<br />

large installations, providing they<br />

are dealt with continuously. It is<br />

unusual to need air traps in sizes<br />

larger than 1/2". Except where a<br />

worn compressor is allowing<br />

lubricating oils to be discharged<br />

with the compressed air, float<br />

operated drainers are the best<br />

choice.<br />

Where the presence in the<br />

system of water/oil emulsions<br />

interferes with the operation of float<br />

drainers, the thermodynamic TD<br />

trap is used. As the TD trap needs<br />

an operating pressure of at least<br />

50 psi when used as an air drainer,<br />

care must be taken when it is used<br />

on small systems. Preferably, the<br />

TD’s should be valved off at start<strong>up</strong><br />

until the system pressure is <strong>up</strong><br />

to 50 psi or more.<br />

Sizing Compressed Air Traps<br />

The amount of water which is to be discharged is determined from<br />

steam table saturated vapor density or estimated with the help of a<br />

graph, Fig. 63 and compression ratio table. An example shows how this<br />

is used.<br />

Example:<br />

How much water will precipitate from 150 cfm of free air at 70°F and 90%<br />

relative humidity when compressed to 100 psig and cooled to 80°F?<br />

Air flow = 150 cfm X 60 = 9000 cu. ft/hour.<br />

From Fig. 63, at 70°F water in air drawn in will be<br />

1.15 X 9000 X 90% = 9.32 lb/h<br />

1000<br />

Determine excess moisture due to compression by dividing hourly air<br />

flow by factor from Compession Ratio Table 20B (page 64), and convert<br />

for (absolute) temperature.<br />

Compression ratio at 100 psig = 7.8<br />

Air volume after compression = 9000 X (460 + 80) = 1175 cu. ft./h<br />

7.8 (460 + 70)<br />

From Fig. 63, 1000 cu. ft. at 80°F can carry 1.6 lb. of water.<br />

1175 cu. ft. will carry 1175 X 1.6 = 1.88 lb/h<br />

1000<br />

So, (9.32 lb. – 1.88 lb.) = 7.44 lb/h of water will separate out.<br />

Figure 63: Moisture Holding Capacity of Air at Varying Temperatures<br />

Pounds Water Vapor per 1,000 cubic ft. at Saturation<br />

3.0<br />

2.8<br />

2.6<br />

2.4<br />

2.2<br />

2.0<br />

1.8<br />

1.6<br />

1.4<br />

1.2<br />

1.0<br />

.8<br />

.6<br />

.4<br />

.2<br />

0<br />

-20 -10 0 10 20 30 40 50<br />

Air Temp °F<br />

60 70 80 90 100

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