Thanks Little Inch, I'll be updating this. Probably post it in a new thread.
I'm getting married tomorrow so I can't do it this soon.
BTW, its supposed to be a 4M diameter Tank, not an inch. lol, my Bad. :)
Kind Regards to everyone here.
Ericson
Yes, I was thinking about that too, though in theory only, as I do not really know how to calculate it. I haven't calculated flow diversions before. I do mostly calculating the correct pump to use by way of Equivalent length. But again, I haven't really tried knowing the exact flow rate when a...
I would like to apologize to Mike for the irresponsible statement.
Here is an attached Sketch of the System.
Its a one step transfer to another open tank process. However, my problem is that I want to divert some of the flow to serve a dilution to an open pit.
The Sketch is just a...
Hi Guys,
I know my question may be fairly easy for the professionals, but I would like to pose this topic and see how it goes.
The Problem:
Say I have a centrifugal pump the pumps water to a open tank that is 4"dia x 5m height.
And I will need to tap a 2"dia pipe to its discharge pipe...
BigInch, yes the flow is very much within the range of the pump curve's BEP. I'm going to try and post the pump's curve later.
I have another question though..
why do they say that you will save more power if you operate the centrifugal pump near BEP?
Say a centrifugal pump with a control valve...
LittleInch, I think what your describing is the efficiency of the VFD? If that is it, then yes, actually I do multiply an additional 90% eff for the VFD, when calculating for the Power. Say, Pump eff * Motor eff * VFD eff. BTW, I got to download the file this time, thanks again. Also, about the...
Ok you guys, thank you for giving your time on this.
Little inch, I agree with you with regards to your explanation of the system curve. So this means that even though i calculated the Total Dynamic Head to be 32M, I only need 20 meters of head with a VSD to get 190m3/hr?
Additional info to...
Hi there fellow engineers,
I have a question with regards to a system with a throttled valve.
First let me explain the system,
A centrifugal pump supplies stock (3.5% consistency) to the top of Chest B, from Chest A (both chest are open to the atmosphere).
The Levels on both chest are...
