1. Pump Curve from catalogue, pump curve 會顯示個pump既Pressure Head & Flow Rate, 個Pressure Head 去到極限,個Flow Rate就會係零。當然我地都要用條System Curve碰埋去,睇下點Match Design Point
2. 睇下用幾多Power
4. 睇下個Net Positive Suction Head NPSH夠唔夠,有分NPSHA & NPSHR (A for Available, R for Requried)
NPSHA - 個泵Inlet嗰點既Pressure
NPSHR - 個泵需要既Pressure,呢個Pressure要係足以被免被Cavitation破壞
NPSHA > NPSHR + 0.6m
根據ASHRAE Handbook 2016 - HVAC Systems and Equipment Chapter 44 Centrifugal Pumps, NPSHA大唔得過NPSHR的話,就會有cavitation, noise, 為免麻煩做設計時最好大得過;尤其係cooling tower呢類open system更加要注意。
5. 仲有其他換impeller size, 改泵速,用VSD等以致條pump curve 改變可以參考下
鳴謝﹕紅豆
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