1.4Technical conventions
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Dynamic viscosity | µ |
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| mPa.s = cP (Centipoise) | |
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Kinematic viscosity | ν = µ |
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| ρ |
| ρ = density | — 3 |
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| mm2 |
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| ν = kinematic viscosity [ | |
Note! In this manual only dynamic viscosity is used. |
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Pressure | p | [bar] |
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| ∆p | Differential pressure = [bar] | |||
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| pm | Maximum pressure at discharge flange (design pressure) = [bar] | |||
Note! In this manual, unless otherwise specified - pressure is relative pressure [bar]. | |||||
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Net Positive | NPSHa | Net Positive Suction Head is the total absolute inlet pressure at | |||
SuctionHead |
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| the pump suction connection, minus the vapour pressure of the | |
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| pumped liquid. | |
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| NPSHa is expressed in meter liquid column. | |
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| It is the responsibility of the user to determine the NPSHa value. | |
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| NPSHr | Net Positive Suction Head Required is the NPSH determined, | |||
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| after testing and calculation, by the pump manufacturer to avoid | |
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| performance impairment due to cavitation within the pump at rate | |
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| capacity. |
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| The NPSHr is measured at the suction flange, at the point where | |
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| the capacity drop results in a pressure loss of at least 4%. | |
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Note! In this manual, unless otherwise specified, NHPH = NPSHr
When selecting a pump, ensure that NPSHa is at least 1 m higher than the NPSHr.
A.0500.551 – | 11 |