Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Head Determination Of A Centrifugal Pump Having Large Number Of Parall


This topic has been archived. This means that you cannot reply to this topic.
2 replies to this topic
Share this topic:
| More

#1 ayan_dg

ayan_dg

    Gold Member

  • ChE Plus Subscriber
  • 148 posts

Posted 30 June 2008 - 12:39 AM

How to find the required head of a centrifugal pumps which have a huge number of parallel consumers like Potable water supply pump. In my case the total consumers are thirty ! the general method which I was following was to find the longest route from pump discharge header which have the largest pressure drop but as the flow & line sizes are changing due to large number of consumers in between it is becoming an awfully tedious exercise. Can anyone suggest a quicker method ?

#2 JoeWong

JoeWong

    Gold Member

  • ChE Plus Subscriber
  • 1,223 posts

Posted 30 June 2008 - 06:52 AM

QUOTE (ayan_dg @ Jun 30 2008, 01:39 AM) <{POST_SNAPBACK}>
How to find the required head of a centrifugal pumps which have a huge number of parallel consumers like Potable water supply pump. In my case the total consumers are thirty ! the general method which I was following was to find the longest route from pump discharge header which have the largest pressure drop but as the flow & line sizes are changing due to large number of consumers in between it is becoming an awfully tedious exercise. Can anyone suggest a quicker method ?


Pressure drop along the line (any branch) can be fixed by the unit pressure drop criteria i.e. 2 bar/km. Thus for main header and branches will expect consistent unit pressure drop. Note : sometime the main header and branch may have different unit pressure drop criteria.

Find the distance for furthest user (i.e. 200m), time the targeted unit pressure drop (i.e. 2 bar/km), you will get the pressure required at the pump discharge.

Once you have fix first round all the pressure profile, it can be further optimized.

Above is just one of the fastest way to fix pressure profile and pump head.

#3 gvdlans

gvdlans

    Gold Member

  • ChE Plus Subscriber
  • 619 posts

Posted 30 June 2008 - 08:50 AM

... or use dedicated software such as Pipenet standard module (see http://www.sunrise-s...dard_module.asp ) or FluidFlow ( http://www.fluidflow...w/FluidFlow.asp )




Similar Topics