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## Main Question or Discussion Point

Hi i'm currently writing a some software for calculating the effects of

differant grades of water on Centrifical Pump Purformance

i have be able to calculate all the apropiate Pressures, flows, viscositys, density, and pressure loss effects on the pump purformance

where i'm having trouble is in calculation of NPSH(a) (net positive suction head),

however to calculat this correctly i need to know the vapor pressure of the water that if feeding the pump

using the following formula

NPSHa = Fluid Surface Pressure (atompheric pressure as fluid surface)

+ Suction Head

+ Guage Pressure at Fuild Surace (almost always Zero)

- Suction Pipe friction Losses

- Fluid Vapour Pressure

however its simple enuf to fin the vapour pressure of water at a given temp just using the

Antoine equation

(with Temp Range of 0 - 100c)

vP = 10 ^ (A -(B/C+T))

where

A = 8.07131

B = 1730.63

C = 233.426

T = Temp C

however i now want to adjust the Vapour pressure to match the not so pure water

i wish to addin the effect of the salinity to calculate the correct vapour pressure

i can enter the salinity as EC, PPT, PPM or PSU (and convert between then accuratcy or +- 1%, with my own made up equation as i couldn't find one to do it)

So after all that background

First thing i need to know is that my EC to PSU, PPT calculator only works when messuring at 25c

if i rase the temp does the EC change... if so is it enough to worry about?

and is there a formula to help calculate this

And second and most important is there an equation to correct the vapour pressure based on the EC, PPT, or PSU?

or denisty of the water

Hope the questions make sense, and thanks up front for the help

differant grades of water on Centrifical Pump Purformance

i have be able to calculate all the apropiate Pressures, flows, viscositys, density, and pressure loss effects on the pump purformance

where i'm having trouble is in calculation of NPSH(a) (net positive suction head),

however to calculat this correctly i need to know the vapor pressure of the water that if feeding the pump

using the following formula

NPSHa = Fluid Surface Pressure (atompheric pressure as fluid surface)

+ Suction Head

+ Guage Pressure at Fuild Surace (almost always Zero)

- Suction Pipe friction Losses

- Fluid Vapour Pressure

however its simple enuf to fin the vapour pressure of water at a given temp just using the

Antoine equation

(with Temp Range of 0 - 100c)

vP = 10 ^ (A -(B/C+T))

where

A = 8.07131

B = 1730.63

C = 233.426

T = Temp C

however i now want to adjust the Vapour pressure to match the not so pure water

i wish to addin the effect of the salinity to calculate the correct vapour pressure

i can enter the salinity as EC, PPT, PPM or PSU (and convert between then accuratcy or +- 1%, with my own made up equation as i couldn't find one to do it)

So after all that background

First thing i need to know is that my EC to PSU, PPT calculator only works when messuring at 25c

if i rase the temp does the EC change... if so is it enough to worry about?

and is there a formula to help calculate this

And second and most important is there an equation to correct the vapour pressure based on the EC, PPT, or PSU?

or denisty of the water

Hope the questions make sense, and thanks up front for the help

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