![pipesim 2007 pipesim 2007](https://www.aimspress.com/aimspress-data/aimse/2021/2/PIC/energy-09-02-019-g010.jpg)
Engineered Software refused to deal with it until we got the client (big fish) involved and they threw their weight around (as in client specific patches were given). This performance issue, in my opinion, had nothing to do with calculation complexity. There was an unfortunate performance cliff introduced with Pipe-Flo 12 with the redesign of the engine, it got better in 14, pushed much higher in 15, and as far as I can tell removed in 16. I can say that 2007/2009 versions will be fine MOST LIKELY, Pipe-Flo 12/14 will struggle, Pipe-Flo 15 MAY work, and Pipe-Flo 16 will be completely fine. At "1000" pipes, and thus thousands of nodes, lots of inline devices, etc.
![pipesim 2007 pipesim 2007](https://i.ytimg.com/vi/7V7rASXfQjo/sddefault.jpg)
Would I most likely have to separate the system into sections so the software/computer can handle it? Thanks!ĭepends on your version. If this is just air or a cooling water network, holy crap, use Pipe-Flo. In your case, you better have a GOOD REASON to use HYSYS in order to use HYSYS. I've found HYSYS's hydraulic modeling from a pressure drop standpoint to be "secondary" to it's function. If you have any kind of "repetition" to the model or network, then Pipe-Flo will be even faster. I've used HYSYS quite a bit and Pipe-Flo extensively, and if you have a single fluid systems and don't have any complex thermo behavoir, recycle loops, and aren't flashing anything, then with the limited amount of information given I can emphatically say pipe-flo will be an ORDER OF MAGNITUDE (possibly 2) quicker at what you need to do.
![pipesim 2007 pipesim 2007](https://saneibook.com/media/image/49503/0049503.jpg)
HYSYS is capable of dynamic modeling as well, Pipe-Flo allegedly has a dynamic modeler but I have not used it. What's the fluid? Water? Clean Dry Air? Nitrogen?ĭo you have a need for any kind of complex thermo along the way, particularly any fluids that are prone to flashing, or for say mixtures of different components for which you don't have any thermo data, do you need to model unit ops along the way, things like gas/liquid separators, or heat exchangers? Do you have recycle loops? HYSYS will also be better at "seeking" specific model states through "setpoint" behavior, Pipe-Flo has nothing that works that way. LearnEngineering: Learn & discuss engineering concepts.EngineeringStudents: For wee engineerlings./u/_wampa_stompa: Sheet metal, Structural, Aerodynamics (AE)ĭirectory of Useful Subreddits Engineering Fields./u/unbelieverben: Plastics/Molding (CHE), Glass (Display/Automotive)./u/theaeroengineer: Aircraft Design (AE)./u/Saryu: IP Video Distribution (EE/SE)./u/rockitscyentist: Control Systems (AE)./u/lafleur818: Environmental/Wastewater.
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#Pipesim 2007 how to#
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