A relationship can be drawn for many components between flow energy and flow rate. This can be a decrease (e.g., a loss across a valve) or increase in energy (e.g. energy added by a compressor). The specific parameter used to represent flow energy can vary depending on application. It can be given in terms of pressure change or head change, and there is a critical difference between the two.

Consider a centifugal turbomachine (a pump or radial compressor): Kinetic energy is imparted to the fluid by accelerating it along the radius of the impeller. If the rate of rotation is held constant, a denser fluid will have more energy imparted to it than a lighter weight fluid. This would give rise to higher pressures. In other words, the pressure change depends on the density of the fluid.

Sometimes curves are provided in terms of head. This is convenient because head is a unit of specific energy - or energy per weight. Therefore, it does not vary with fluid density like pressure does. The head added to a fluid by a pump or compressor at a fixed speed, for example, will be the same for fluids of different densities.

However, head relationships are not always available or meaningful. If a pressure vs flow relationship is used, a reference density must be specified. This is the fluid density used during testing and creation of the curve.

Note: Incompressible liquids are used in the example in Figure 1, but the principles apply similarly to compressible flow.

Affected Parameters

There are several parameters that are affected by the density of the fluid:

• Pressure - As discussed above
• Mass Flow - The mass term contains information about the density of the fluid
• Power - More power is demanded by a compressor to meet the head curve for a denser fluid. While head is independent of density and therefore often reported by manufacturers, power is not independent of density. Therefore, a proper specification sheet that includes power must also include the reference fluid density.

Accounting for Reference Density

Compressors and any Resistance Curve allow for the specification of a reference density if one of the above parameters is selected. The selection appears below the curve fit area as shown in Figure 2.

There are two options:

• No Correction (default) - This selection assumes that the component was tested with the fluid defined in the Fluid Panel and is operating at the reference conditions.
• User Specified - This directly specifies the reference density. If the fluid or operating conditions differ from the testing conditions, the entered curve will be corrected.