-
-
November 21, 2023 at 10:49 am
Mark Boots
SubscriberHi,
I'm currently working on a project where I have to design a dredge system (very simple by using the venturi effect to create a suction at the suction inlet by positioning 2 jets that accelerate the flow). I am changing the geometry and trying to discover what the influence of these changes is on the suction inlet velocity. One aspect that I have to investigate as well, is the use of different pumps that operate at the same power but have different amount of stages which results in high flowrate and lower head or higher head and lower flow rate.
In the picture below my geometry can be seen. I use an operating condition of 1 atm, at the suction inlet 0 Pa gauge pressure, at the outlet 0 Pa pressure and at the jets I convert 16 m^3/h to corresponding velocity. I want to use pump-curve data at the jet inlets.
Now my problem: I have trouble with understanding how I can impose the correct boundary conditions when I only know the inlet pressure and inlet velocity. Because using a pressure inlet results in too high flow rates and using Q=16 m^3/h as velocity inlet (v = Q / A / 3600), my pressures are too low.
Question: Which steps do I have to take in order impose a the jet a flow rate of 16m^3/h and a pressure of 11 bar?
Please can some help me? Thanks in advance!
-
November 21, 2023 at 11:43 am
Rob
Forum ModeratorIf the fluid isn't compressible you only get one of flow or pressure. Also note, a 2d system is nominally a 1m thick domain and in reality you may be looking at pipes so a direct comparison with experimental data may be difficult.
-
November 21, 2023 at 12:56 pm
Mark Boots
SubscriberYes, the fluid is incompressible. I do understand that comparing a 2D system to experimental data might not be precise, but I don't understand why well pump manufactures advertise with pumps with either a large head or a large flow. Because two different pumps can operate on the same flowrate, while one can produce a larger head then the other.
Maybe I need to rephrase my question then to "Is it possible to compare two pumps in Ansys with the same flow rate but with a different head?"
Do I have to change the outlet pressure or is only one solution possible (when connecting two different pumps with the same flow rate to the same jet-inlet)?
-
November 21, 2023 at 2:03 pm
Rob
Forum ModeratorIn reality the pump will spin/compress to push water through at a speed and with a certain pressure. If the losses in the pipework are low, the pump may deliver more flow, or the same flow for a lower speed/power draw.
In Fluent we tell the system we want some flow rate. The solver will then deliver that, and alters the inlet pressure until the desired flow is acheived. We can then look at the pump curve(s) to see what will deliver that pressure and flow, and if there are options which does it for a lower power draw.
-
November 21, 2023 at 2:09 pm
Mark Boots
SubscriberOf course, I know enough for now. Thanks a lot for you help!
-
- You must be logged in to reply to this topic.

Boost Ansys Fluent Simulations with AWS
Computational Fluid Dynamics (CFD) helps engineers design products in which the flow of fluid components is a significant challenge. These different use cases often require large complex models to solve on a traditional workstation. Click here to join this event to learn how to leverage Ansys Fluids on the cloud, thanks to Ansys Gateway powered by AWS.

Earth Rescue – An Ansys Online Series
The climate crisis is here. But so is the human ingenuity to fight it. Earth Rescue reveals what visionary companies are doing today to engineer radical new ideas in the fight against climate change. Click here to watch the first episode.

Ansys Blog
Subscribe to the Ansys Blog to get great new content about the power of simulation delivered right to your email on a weekly basis. With content from Ansys experts, partners and customers you will learn about product development advances, thought leadership and trends and tips to better use Ansys tools. Sign up here.
- Floating point exception in Fluent
- What are the differences between CFX and Fluent?
- Heat transfer coefficient
- Difference between K-epsilon and K-omega Turbulence Model
- Getting graph and tabular data from result in workbench mechanical
- The solver failed with a non-zero exit code of : 2
- Time Step Size and Courant Number
- Mesh Interfaces in ANSYS FLUENT
- Suppress Fluent to open with GUI while performing in journal file
- error: Received signal SIGSEGV
-
8740
-
4658
-
3151
-
1678
-
1452
© 2023 Copyright ANSYS, Inc. All rights reserved.