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Energy saving in compressed air systems - Norgren Pneumatics ...

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How to improve energy efficiency<br />

Double act<strong>in</strong>g cyl<strong>in</strong>ders are usually applied to give a power stroke <strong>in</strong> one direction but<br />

simply return the piston rod <strong>in</strong> the other direction. If the control valve is connected to a<br />

s<strong>in</strong>gle supply pressure, the return stroke will be at the same pressure as the power stroke<br />

thereby wast<strong>in</strong>g energy.<br />

Where large bore, long stroke or multiple cyl<strong>in</strong>der <strong>systems</strong> exist, considerable <strong>sav<strong>in</strong>g</strong>s<br />

can be made. Use a pressure regulator to reduce the return stroke pressure. Where<br />

several cyl<strong>in</strong>ders are <strong>in</strong>volved, a s<strong>in</strong>gle pressure regulator could feed a common low<br />

pressure supply to the changeover valves. Use control valves that can be reverse<br />

connected to provide dual supply port<strong>in</strong>g (figure 7). Average <strong>air</strong> consumption <strong>sav<strong>in</strong>g</strong> can<br />

be measured us<strong>in</strong>g the formula:<br />

π (D 2 - d 2 ) x L x (CR1 - CR2) x N<br />

4 = <strong>sav<strong>in</strong>g</strong> <strong>in</strong> scfm,<br />

1728<br />

Where:<br />

D = cyl<strong>in</strong>der diameter (<strong>in</strong>)<br />

d = piston rod diameter (<strong>in</strong>)<br />

L = stroke length (<strong>in</strong>)<br />

CRx = compression ratio = (Px + 14.7)/14.7<br />

P1 = applied pressure (psig) - outstroke<br />

P2 = applied pressure (psig) - return stroke<br />

N = cycles per m<strong>in</strong>ute<br />

Pressure drop<br />

Figure 7: Reverse connected<br />

valve with dual supply<br />

pressures<br />

Pressure drops <strong>in</strong> a system are caused by resistance to flow by localized restriction and<br />

general friction <strong>in</strong> pipes and components. A distribution system constructed from large<br />

bore pipe keeps the velocities low therefore the friction low.<br />

Work<strong>in</strong>g velocities should be under 20 ft/s <strong>in</strong> ma<strong>in</strong> l<strong>in</strong>e. Increas<strong>in</strong>g the source pressure to<br />

compensate for undersized <strong>systems</strong> <strong>in</strong>creases <strong>compressed</strong> <strong>air</strong> production costs. Every<br />

14.5 psig of unnecessary pressure drop leads to an <strong>in</strong>crease of 7% <strong>in</strong> generat<strong>in</strong>g costs.<br />

Pipe rout<strong>in</strong>g should have gentle sweep<strong>in</strong>g bends where possible. An elbow fitt<strong>in</strong>g has<br />

resistance equivalent to 5.2 ft of straight pipe. Use ball valves at isolation po<strong>in</strong>ts. These<br />

have an equivalent resistance of just 1.3 ft of straight pipe, less than half the resistance of<br />

a gate valve. When select<strong>in</strong>g primary components such as filters, it is important to have<br />

units large enough to realise no more than 1.5 psig pressure drop (with a new element) at<br />

the desired work<strong>in</strong>g flow rate.<br />

Page 6 of 8

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