BOSpulse 6.1 Release – Questions and Answers

Table of Contents

Gas properties

When using the AGA-8 (GERG-2008) equation of state, the viscosity can be either specified explicitly as a piece-wise linear function of the temperature, or calculated by BOSpulse. In the latter case the per-component gas viscosity is calculated with Sutherland’s law. The component values are combined by means of the Herning and Zipperer method to obtain the viscosity of the compound gas.

Reciprocating compressor modelling

We use pipe elements to model gas passages. We adjust the acoustic length to obtain the correct acoustic dimensions and volumes. The acoustic dimensions and pipe volumes tend to be the two most important parameters when modelling a gas passage. BOSpulse comes with an example model, named “API618Assessment”, that features a model of a compressor including the gas passage. The construction of this model is explained in more detail in this series of webinars.

No, unfortunately detailed valve data are not available in the Ariel data files. When importing such a file into BOSpulse, the compressor valves will be modelled as ideal valves.

Multiple cases, parameter studies and batch analysis

You can do that manually, through the script interface or through the Ariel compressor import interface.

Yes indeed, the size of the parameter space will increase very rapidly with the number of compressors. To restrict the parameter space, you could vary each phase shift in a crude way, say with four or maybe eight steps. After that, you could apply a custom parameter schedule to zoom in on the locations in the parameter space that lead to the largest pulsations or shaking forces.

An alternative approach might be to analyse each compressor separately in a different scenario (set one compressor active, and unload or deactivate the other compressors). Then you could combine the results from the different scenarios, either by using a virtual case, or by means of some spreadsheet manipulations. In the latter case you can use the custom report function to get the results from each scenario into a spreadsheet.

You can perform a (multi-dimensional) parameter study and/or use virtual cases to combine results from multiple scenarios.

You typically do so by means of multiple scenarios in which you modify certain aspects of a model. You can also deactivate certain parts of a model in a scenario.

Pumps and liquid service

You can model rotary lobe and other positive displacement equipment in BOSpulse by means of a periodic flow boundary condition. This requires that you know the flow profile within one time period. The new BOSpulse release supports non-Newtonian liquids.

Analysis types and structural modelling

Yes. I can also explain how the new Junction Activation parameter works. The pressure source amplitudes are based on an analytical model described in literature. Note that BOSpulse assumes that pulsations are only significant if they excite natural acoustic modes in a system.

Yes, you can include supports and beam elements in a piping model. These will be accounted for when performing a structural analysis by means of the ANSYS interface. You can also export the beam elements to CAESAR II.

BOSpulse focuses on periodic flow conditions. We have another application, named BOSfluids, that focuses on steady state and general transient flow conditions.

Results and reporting

You can select multiple data sets when generating a custom report. You also get information about unfiltered peak-peak pressure pulsations if you have specified an allowable limit for them.

Maybe a Profile Plot is what you are looking for?

Will BOSpulse run on a Windows 7 HP workstation?

Probably not, but you could try it. A trial version of BOSpulse can be downloaded from our website. You can also try running BOSview (also available from our website). If that program runs correctly, then BOSpulse probably will too. We develop our applications for Windows 11, as that is the operating system currently supported by Microsoft.