Sizing pump head
Sizing pump head
(OP)
What refernce are you using for fittings equivalent lenght?
Also do I consider each valves when calculating the total head?
Pipe lenght, fittings, coil press drop, valves (?) --- are this the information i need when do pump head?
Thank you in advance.
Also do I consider each valves when calculating the total head?
Pipe lenght, fittings, coil press drop, valves (?) --- are this the information i need when do pump head?
Thank you in advance.





RE: Sizing pump head
Yes, you need to calculate each and every pipeline, fitting, valve, heating coil, boiler etc. to get information about branch with highest pressure drop to be able to determine pump head.
In some projects you could add percentage for fittings instead of calculating each and every fitting, but you should have sufficient experience to get a feeling.
For other elements, especially valves and coils, such rules of thumb are even less desirable.
RE: Sizing pump head
I use an excel spreadsheet. The main components, in my opinion that need to be accounted for are: Length and size of piping, chiller or boiler pressure drop, control valve, air separator, triple duty valve and suction diffuser and the coil pressure drop of the heat transfer device at the end of the run(reheat coil, Unit ventilator, fin tube, AHU coil, etc). These values are easily obtainable from the manufacturers of the equipment you design around. As for all the fittings, sometimes this is not as practicle to get so I typically take the pressure drop of the total piping run and add 50% for fittings (ie if the piping pressure drop is 22 feet then add another 11 feet for the fittings).
Like I said, Everyone has their own methods, but this method has never gotten me in trouble.
I hope this helps.
RE: Sizing pump head
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: Sizing pump head
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: Sizing pump head
RE: Sizing pump head
Properly, Total head is made up of:
1. net elevation change from supply point to discharge point
2. net external pressure (if any) applied to the liquid.
3. Frictional losses in piping, valves, fittings, etc.
4. Entrance and exit losses at supply and delivery point respectively.
5. difference in velocity heads at pump discharge and pump suction.
The first two terms together make up the static portion of total head and do not change with the flow through the system.
The remaining 3 terms are lumped together as friction head and vary with flow (pressure increases as the square of the flow increase). Most HVAC calculations can ignore the 4th and 5th terms as they are typically too small to make a difference.
RE: Sizing pump head
RE: Sizing pump head