Search found 359 matches

by admin
Sat Nov 25, 2017 1:44 pm
Forum: Flow calculators and fluid flow problems
Topic: equivalent length
Replies: 1
Views: 136

Re: equivalent length

You can find one on the left side menu called K factor - fittings.
by admin
Tue Apr 04, 2017 6:52 pm
Forum: Flow calculators and fluid flow problems
Topic: Flow between the Vessels
Replies: 3
Views: 1175

Re: Flow between the Vessels

I have used my calculator for gas flow on pipeflowcalculations.com. As you say the fluid is air than one can use air pressure drop calculator available on the same web site. I have divided the process into segments: A. What I have done is calculate flow rate for 12 bar inlet and 6 bar outlet. B. Aft...
by admin
Sat Apr 01, 2017 8:06 am
Forum: Flow calculators and fluid flow problems
Topic: Flow between the Vessels
Replies: 3
Views: 1175

Re: Flow between the Vessels

This type of calculation requires differential equation solution, meaning it is not an easy task, because the pressure on the exit of the pipe line is changing from 6 bar to 12 bar, and flow through connecting pipeline slows every moment. As you want to fell 5000 m3 tank through 1" pipe - I can tell...
by admin
Sat Apr 01, 2017 7:35 am
Forum: Flow calculators and fluid flow problems
Topic: Thrust from open gas line?
Replies: 2
Views: 783

Re: Thrust from open gas line?

It is density x velocity^2 x area
by admin
Fri Jul 08, 2016 7:09 am
Forum: Flow calculators and fluid flow problems
Topic: Gas discharge flow calculator
Replies: 2
Views: 2388

Re: Gas discharge flow calculator

Try with gas pressure drop calculator. It will work ok for your problem.
by admin
Tue Jun 28, 2016 7:55 am
Forum: Flow calculators and fluid flow problems
Topic: Calculating Pressure Drop in Natural Gas Piping
Replies: 1
Views: 1321

Re: Calculating Pressure Drop in Natural Gas Piping

Hi,
Yes. That formula is ideal for your problem.
You are also free to download and try natural gas calculator that will help you on the calculation.

If you give me actual flow rate or burner power I can help you on calculation.
by admin
Sun Jan 03, 2016 10:28 am
Forum: Flow calculators and fluid flow problems
Topic: New calculator available - Bernoulli equation
Replies: 0
Views: 1814

New calculator available - Bernoulli equation

Bernoulli equation calculator is now available. Go to Bernoulli equation calculator Bernoulli equation is the most important equation for engineering analysis of flow problems. Most practical tasks are resolved by direct implementation of Bernoulli equation with its corresponding condition - continu...
by admin
Sat Nov 21, 2015 10:49 am
Forum: Flow calculators and fluid flow problems
Topic: Venturi tube and nozzle calculators available
Replies: 0
Views: 1639

Venturi tube and nozzle calculators available

Venturi tube and nozzle calculators are available on pipeflowcalculations.net web site that works like web application without the need to install and use plug-in. You can find calculators at: Venturi tube and Nozzle calculator Tell me what do you think about them using contact page on the same web ...
by admin
Mon Oct 12, 2015 7:34 pm
Forum: Flow calculators and fluid flow problems
Topic: Three most wanted calculators redesigned on pipeflowcalculations.net
Replies: 0
Views: 1721

Three most wanted calculators redesigned on pipeflowcalculations.net

Top three calculators are now available as web application, meaning that on user side, nothing is required else but modern web browser, Internet connection and decent PC or mobile device. Pressure drop calculator, pipe diameter calculator, orifice flow calculator are now available on pipeflowcalcula...
by admin
Mon May 11, 2015 10:59 pm
Forum: Flow calculators and fluid flow problems
Topic: passive pressure compensation: time to equalise
Replies: 4
Views: 2539

Re: passive pressure compensation: time to equalise

I think so. Yet, as I said I haven't got back confirmation of the derivation that you used also, but all calculation results are very close to the conclusion that you made. 1.35 m is about 13.5 kPa, so as you have +/- 50 kPa that should be with solid reserve, which I think is ok and should be accept...