Introduction

In this guided exploration (DTNN-3) on positive displacement compressors, we detail the calculation and sizing of a piston compressor used to supply a compressed air storage tank.

Note that a second guided exploration (DTNN-1) deals with the determination of the surface of a heat exchanger and its behavior in off-design conditions.

Functionally, compressors are devices used to increase the pressure of fluids passing through them.

They are used for many industrial applications, for refrigeration, air conditioning, transportation of natural gas ...

Technologically speaking, compressors can be grouped into two main classes:

• Positive displacement compressors, in which the fluid is trapped in a closed volume which is reduced gradually to achieve compression;

• And dynamic compressors, which use a different principle: the compression is obtained by converting pressure into kinetic energy imparted to the fluid by moving blades.

For further explanations, we suggest you refer to the page of the Thermoptim-UNIT portal which deals with positive displacement compressors. https://direns.minesparis.psl.eu/Sites/Thopt/en/co/compresseurs-volum.html

We must specifically mention air compressors, used as a source of power in public works and construction and in factories, pneumatic tools having many benefits. The example presented here focuses on this type of device.

The example we are dealing with here is intended to diagnose the problems and show how they can be resolved without the overall system being too complicated. For specialists, it will seem a bit simplistic, but for beginners it is already quite difficult to treat completely.

Typology of problems posed and associated difficulties

The study of the compressors in an energy system has very different levels of difficulty depending on the objectives that we pursue.

The most basic approach is to calculate the outlet temperature when the compression ratio and isentropic efficiency are known. If the flow-rate involved is also known, the compression work can be deduced directly.

The inverse problem is solved also simply: knowing the compressor inlet and outlet states, you can determine the isentropic efficiency of the device.

To go further and determine the isentropic efficiency and the flow through a given displacement machine, we have to perform more complicated calculations, requiring a thorough knowledge of compressor operation.

We will call sizing calculations for determining the displacement of a compressor knowing the laws giving its volumetric and isentropic efficiencies.

This is by the way a general problem in energy systems studies: as long as one is satisfied to carry out cycle studies without trying to size the geometry of the components, the calculations are much simpler than when one wishes to closely analyze their internal behavior.

Once the displacement determined, allowing to geometrically characterize the compressor, another problem remains to be treated: that of its behavior when operating conditions differ from those used in the design.

We call this problem the study of its off-design behavior.

It can be a higher level of complexity than the sizing, because it may require solving large systems of nonlinear equations when several components are coupled together.

This is a relatively complex problem that you should understand before you can use it. It is presented in this page of the Thermoptim-UNIT portal, which we strongly recommend that you read before anything else.

When trying to accurately represent the behavior of a given compressor, it is necessary to characterize it by:

• Its displacement;
• The law of volumetric efficiency;
• The law of isentropic efficiency.

The theory shows that the main factor on which these quantities depend is the compression ratio Pref/Pasp, ratio of the discharge pressure to the suction pressure.

Generally, a first order polynomial law is enough to represent the evolution of the volumetric efficiency as a function of the compression ratio.

To properly represent the isentropic efficiency eta, we need more parameters. The law we will retain uses 5:

To size a compressor, it is necessary to know these laws.

Identification of their parameters can usually be made on the basis of data provided by the manufacturer.

Implementation in Thermoptim

Versions 2.7 and 2.8 of Thermoptim allow sizing and off-design studies. For this, they introduce screens complementary to those which allow the usual phenomenological modeling to be carried out.

They define the geometric characteristics representative of the different technologies used, as well as the parameters necessary for calculating their performance. For a given component, they obviously depend on the type of technology chosen.

The calculations are carried out in extensions of the core of the software package, and in particular in programs called controllers of Thermoptim.

They are so called because they take control of the software by driving it to perform specific operations not available in the core screens.

There are many types of controllers. Two categories of controllers make it possible to carry out sizing studies, generic controllers and specific controllers.

The former are by nature multipurpose but can only perform simple calculations, while the latter, defined specifically for a particular model, can perform much more complex operations.

Loading the cooled displacement compressor model

Loading the model

Click on the following link: Open a file in Thermoptim

If you display the values ​​in the diagram editor, you get the synoptic view below.

The compressor screen is given below.

The setting of this model is completely classic and does not require any particular explanation.

The only remark at this stage is that the flows were entered in kg/s and not in g/s, whereas Thermoptim would allow to do so.

This method is necessary because Thermoptim carries out sizing studies using the units of the International SI System.

Compressor sizing

To size the compressor, we must have the parameters of the equations giving the volumetric and isentropic efficiencies.

We assume here that they have been determined from data provided by the manufacturer.

The calculation of the compressor corresponds to the steps below:

• the volumetric and isentropic efficiencies lambda and eta are calculated from their equations
• If you know the rotation speed (in rpm), the displacement and the volumetric efficiency, the flow rate can be calculated: Vvol = lambda N Vs / 60
• Knowing the density at the inlet v, we deduce the mass flow: m = Vvol / v = lambda N Vs / 60 /v

In design mode, we determine the rotation speed to provide the desired flow or the displacement corresponding to a given rotation speed. The calculation is performed taking into account the inlet and outlet pressures and the flow value entered in the flow-rate field of the compressor.

In off-design mode, the compression ratio determines lambda and eta, which gives the compressor flow rate and outlet temperature.

Procedure to be implemented

Using the generic controller

Loading the generic controller

The generic sizing controller can be loaded from the simulator screen. To do this, activate the "Controller frame" line in the "Special" menu.

Then select the line "generic sizing controller" from the list of available controllers, and click "OK".

The controller screen opens. Click on "Set the sizing screens".

Two rows appear corresponding to the exchanger and the compressor, as in the figure below. Select the one for the compressor.

Its type is by default Compression, and its TechnoDesign VolumCompr. Since it is a positive displacement compressor, they are perfectly suitable. Double-clicking on this line would change the type of TechnoDesign, but this is not necessary here.

Sizing screens are now created.

To access them, return to the simulator screen, and activate the line "sizing screens" in the "Component sizing" menu, or type Ctrl T.

The window allowing access to the existing sizing screens is displayed.

Double-clicking on one of the table rows opens the sizing screen for the selected component.

Sizing screen of a compressor

Here is the sizing screen of a compressor set by default.

The fields on the left side of the compressor sizing screen allow you to enter the compressor characteristics:

• the two volumetric efficiency parameters a0 and alpha;
• the five isentropic efficiency parameters K1, K2, K3, R1 and R2;
• the reference speed (for which the five parameters were determined);
• the swept volume at full load Vs (m3) if it is known, which is not the case here.

Enter in these fields the parameter values, select "Calculate Vs" so that Thermoptim knows that this value must be calculated, then return to the generic controller screen, and click "Design the selected components" after having selected its row.

Once the characteristic values ​​have been entered in these fields, and the "Calculate Vs" option has been selected so that Thermoptim knows that this value must be calculated, return to the generic controller screen, and click on "Design the selected components".

Here is the result you get.

The fields on the right side of the screen show calculated values of isentropic efficiency, mass flow and volumetric efficiency.

The displacement (0.0055 m3) was determined on the basis of the flow entered the compressor process, and other values from the parameter values. Once the displacement is calculated, the "Calculate m" option is selected because it corresponds to the normal calculation mode of this TechnoDesign.

Sizing of the heat exchanger

The sizing of the cooling exchanger is the subject of DTNN-1 guided exploration, to which we recommend that you refer before going further.

Practically, you operate similarly as before. Go to the the sizing screens frame, select the heat exchanger line, click on the "Read settings", and select file "volumComprHxSettings.par". Return to the generic controller screen, select the heat exchanger and click on "Design the selected components".

Here is the result you get.

Off-design calculations

Once the compressor has been sized, its behavior in off-design conditions can be studied by operating in two steps.

• first of all, it is necessary to modify, in the upstream or downstream point of the compressor, the new pressure to take into account. In our case, it is of course the downstream pressure, the compressor sucking air at atmospheric pressure.
  
• then, you must return to the controller screen, and perform a new sizing by clicking on "Design the selected components"
  

The sizing screen is then recalculated.

We will assume that the compressor discharge pressure is now 8 bar and not 5 bar.

Here is the result.

Thermoptim has correctly calculated the new isentropic efficiency and flow rate values, but it has not modified them in the compressor screen and in the air intake screen.

In order for them to be taken into account, they must be copied from the sizing screen to the classic phenomenological screen.

Once these operations have been carried out and the compressor recalculated, the following result is obtained.

The same should be done for the heat exchanger, as explained in the DTNN-1 guided exploration.

In the above, we manually modified the values ​​of the isentropic efficiency and the flow rate, the sizing screen having been constructed by the generic controller. This way of doing things has the advantage that it does not require any programming, but it is a bit long to put into practice when several iterations must be carried out. It would therefore become tedious if you had to simulate the off-design behavior of the exchanger for a wide variation range of its operating conditions.

In this case, it is far better to automate these updates using a specific controller, as we will explain in the next step.

Using a specific controller

Loading the model

Click on the following link: Open a file in Thermoptim

When loading the project, the controller screen opens. Click on "Initial settings" to create the sizing screens and initialize them.

We find the settings made with the generic controller.

Using this controller is much simpler, however.

Just enter the new outlet pressure in this screen so that the whole project is recalculated and updated when you click on the red button "Calculate".

If you return to the diagram editor and double click twice on the F3 key to update the displayed values, you get the following synoptic view.

You can thus modify the input and output parameters of the model and easily calculate the adaptation of the installation to its new operating conditions.

How to program the controller is outside the scope of this guided exploration.

You will find all the explanations on this question in the Thermoptim-UNIT portal, and more particularly in this document.

Conclusion

This exploration allowed you to discover how to size a positive displacement compressor and the corresponding specific settings, using first the generic sizing controller, then a specific controller.

The learning path on the volumetric compressors of the Thermoptim-UNIT portal explains how to use this controller on a practical level. https://direns.mines-paristech.fr/Sites/Thopt/en/co/fil-compresseur-volum.html