Engineering Asked by Ehsan Darrudi on June 15, 2021
I am setting up an irrigation system for my ranch and I have a hard time calculating the minimum pipe pressure requirements to reduce cost. I need to know the maximum pressure the pipe has to cope with. The pipe would transfer water from a high elevated pond (with enough water to feed the line constantly) to a barn down below. There is a 166 meter height difference between the inlet and outlet. I can easily calculate the upper bound pressure as 16.6 bars, however as I get it, the friction loss plays an important role too. The pipe’s length is 1200 meters and made of polyethylene (Absolute roughness of 0.007). We need to open and close the faucet on the exit pint on demand (important) so the water head may reach the full height of 166 meters when the outlet is closed. The question is: do I have to order the 16.6 bar pipe or a lower grade pipe would do?
One way to calculate the pressure drop consist of the following steps:
I'll start from the end. The pressure drop in a circular pipe is:
$$Delta P = lambda cdot frac{L cdotrho}{2 cdot D}bar{u}^2$$
where:
Obviously there are two parameters that are missing in this case:
Given the above we can calculate the average flow velocity as :
$$bar{u}= frac{dot{V}}{A}= frac{dot{V}}{pi frac {D^2} 4} $$ $$bar{u}= frac{ 4 dot{V}}{pi D^2} $$
Therefore the initial equation can be rewritten so that it encapsulates the main two design parameters as :
$$Delta P = lambda cdot frac{L cdotrho}{2 cdot D}left(frac{ 4 dot{V}}{pi D^2}right)^2$$ $$Delta P = lambda cdot frac{ 8 L cdotrho}{pi^2}cdotfrac{ dot{V}^2}{ D^5}$$
Now only pareameter that is not known is $lambda$.
For lambda again the determination of the mean flow velocity is crucial, and the calculation of the Reynolds number. Reynolds will be calculated in this case as:
$$ Re = frac{bar{u} D}{v} = frac{frac{ 4 dot{V}}{pi D^2} D}{v} $$
$$ Re = frac{4 }{pi cdot v}frac{dot{V}}{D} $$
where:
If Reynolds is:
less than 2300 (Re<2300) then the flow is laminar and lambda is calculated as $$lambda = frac{64}{Re}$$
more than 2300 (Re>2300) then the flow is turbulent and lambda is calculated by the colebrook equation (or the Darcy friction factor) as
$$frac{1}{sqrt{lambda}} =-2 lnleft(frac{2.51}{Re sqrt{lambda}} + 0.269cdot frac{k}{D} right)$$
Notice that this equation can be solved iteratively. So you need to assume a value of lambda, e.g. $sqrt{lambda_{assumption}}=1$, then do the calculations on the right hand and arrive at a value for $sqrt{lambda_{calculated}}$, then make the calculated value your new assumption and repeat until the difference between the $sqrt{lambda_{assumption}} $ and $sqrt{lambda_{calculated}}$ is very small.
At this point you should have everything you need to calculate the pressure drop due to friction.
The pressure drop due to height is simply given by:
$$delta P_h = rhocdot g cdot Delta H$$
The total pressure will be given by:
$$Delta P_{total} =Delta P_h + Delta P_{friction} + Delta P_{elements} $$
where:
Although the above is the rough calculation for the pressure drop, IMHO you should go for at least two pumps (one at the base and one at the middle). That will allow you to use more commonly used pipes and avoid expensive and difficult to find components. Also that might lower overall the cost of the pump, and make it easier to procure and maintain. You will probably incur though some initial setup costs.
Answered by NMech on June 15, 2021
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