Fluid Flow and Engineering Software

Accutech 2000 Pty Ltd

 Fluid Flow (Home) |  About Us |  Navigate this site  |  Contact Us

SoftwareSelector:
by application
by name

Downloads
Links
FAQ's
Technical Support
Users
Licensing
CONSULTING
 

 FLUIDFLOW3 Calculation Capabilities
 Previous  Contents  Next  

Engineers using FluidFlow3 can determine the pressure, flow rate and temperature at any point around their pipework system. Any type of system architecture can be modeled, eg open loop, closed loop, branched, etc. Large complex fluid systems can be rapidly analysed allowing “what if" scenarios to be investigated quickly and efficiently. For the flow of gases - expansion, temperature change and choked conditions are all accounted for.

FluidFlow3 will simulate any steady-state pipe network analysis with a single-phase compressible or incompressible fluid with optional heat change calculation at any pipe or equipment item. FluidFlow3 allows different fluids to enter the network at boundaries and will automatically determine the physical properties of the mixture where different streams join.

ANY NUMBER OF FLUIDS WITHIN THE SAME NETWORK

Fluids are specified at each input boundary and the software takes care of composition changes. This means you can analyse networks containing as many fluids as you require. Physical properties of mixtures at flowing conditions are estimated as needed. Networks can also be analysed containing multiple fluids where mixing does not occur. For example, you can analyse cooling water and process streams within the same flowsheet.

Click here for a screen image

FLUID EQUIPMENT

The performance of almost any type of line equipment can be determined, for example:

  • Pump duty, efficiency, NPSH, power
  • Fan or compressor duty
  • Control valve opening
  • Heat change across heat exchangers, pipes
  • Safety relief valves
  • Manual valves
  • Orifice plates
  • Filters
  • Sprinklers and nozzles
  • and much more
TOTAL HEAT BALANCE

Fluid temperatures are specified only at boundary components. All other temperatures as well as fluid phase states are calculated by the software. Temperature effects of pressure changes, heat loss or gain from the surroundings and heat exchange made at each network component make heat transfer an automatic part of network flow calculations.Fluid temperatures are specified at boundary components; all other temperatures as well as fluid phase states are calculated by the software.

COMPRESSIBLE FLOW

Gas calculations make no simplifying assumptions of ideality, adiabatic or isothermal processes etc. Pressure losses are determined by solving the momentum and physical property equations simultaneously. This means more accurate results, particularly at higher Mach numbers.

2-PHASE LIQUID/SOLID FLOW SIMULATION
Non-Newtonian and Settling Slurry

This module is planned for release May 2006. Planned capabilities include:

  • Power Law Fluid correlation - Pseudoplastic, Dilatant (solution according to Darby)
  • Bingham Plastic correlation (solution according to Darby)
  • Yield Pseudoplastic (solution according to Herschel-Buckley or Chilton & Stainsby)
  • Heterogeneous Settling Slurries correlation (solution according to Wasp etc)

The fluids databases will accommodate the necessary data for these simulations such as power law coefficients, particle size distribution, viscometer readings.


2-PHASE LIQUID/GAS FLOW SIMULATION

Currently only liquid mixtures or gas mixtures are allowed. 2-phase liquid/gas will be available end of 2006.

To email us for more information click here


 FLUIDFLOW3 Calculation Capabilities
 Previous  Contents  Next  

 Fluid Flow (Home) |  About Us |  Navigate this site  |  Contact Us  | Top


copyright  disclaimer