Valves with Intercept

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Valves with Intercept

Postby Irrigator » Tue Jul 28, 2009 7:25 am

Hi everybody.

I don’t know the meaning of “valves with intercept” (Headloss equation Intercept (C) Who could help me?

Thanks a lot. Irrigator
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Re: Valves with Intercept

Postby Dan Crosby » Wed Jul 29, 2009 1:16 pm

Hi Irrigator,

The headloss equation for valves is in the form:

    H = KQn + C

    • H = headloss
    • Q = flow
    • K = constant
    • n = index
    • C = intercept

The intercept C represents any headloss in the valve assembly that is not dependent on the flow through the valve. It can be used to introduce a fixed amount of headloss through the valve, but typically there is no flow-independent component to the headloss, and C is zero. However, if you are trying to produce a headloss equation from experimental data, you may find that the curve fits better if an intercept is used. In practice this should not be a problem, provided the valve is only used in flow regimes that are 'on the curve'.

Dan Crosby
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Lincoln Ventures Ltd
PO Box 133, Lincoln
Christchurch 7640

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Re: Valves with Intercept

Postby jovivier » Wed Jul 29, 2009 1:43 pm

The intercept can represent a start-up head required, eg if a valve requires a certain upstream pressure before it will open and the curve cuts the Y-axis instead of going through 0,0.
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Re: Valves with Intercept

Postby Irrigator » Wed Jul 29, 2009 10:47 pm

Fine Dan. Thanks a lot.
Irrigator

Dan Crosby wrote:
Hi Irrigator,

The headloss equation for valves is in the form:

    H = KQn + C

    • H = headloss
    • Q = flow
    • K = constant
    • n = index
    • C = intercept

The intercept C represents any headloss in the valve assembly that is not dependent on the flow through the valve. It can be used to introduce a fixed amount of headloss through the valve, but typically there is no flow-independent component to the headloss, and C is zero. However, if you are trying to produce a headloss equation from experimental data, you may find that the curve fits better if an intercept is used. In practice this should not be a problem, provided the valve is only used in flow regimes that are 'on the curve'.
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Posts: 3
Joined: Sat May 23, 2009 5:29 am


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