This article provides the essential design criteria used to size and select centrifugal gas-liquid separators for steam, compressed air, natural gas and other industrial vapor applications.
To properly size a centrifugal separator the following information is required:
99% efficiency for separation of entrained droplets and particles having a diameter as fine as:
Once the applicable separator design is determined, the model is selected based primarily upon preferred nozzle orientation (in-line or offset) and installation footprint.
The required separator size has three main components. It needs to:
The online separator size calculator supports quick separator sizing and “what-if” comparisons. Separation capacity is calculated in mass and volumetric units for all models. Differential pressure is also calculated so you can quickly toggle separator size until the pressure-drop requirement is satisfied. The calculator includes unit-conversion cells and uses the underlying polynomial formulas for greater precision than printed charts.
There are two calculators: one for steam applications and one for all other gases.
Steam: Required inputs are minimum operating pressure (PSIG) and maximum mass flow rate (lbs/hr). If steam quality is known, enter it; otherwise the default value of 95% is used.
Two sizes are calculated: Standard Separator Size and Receiver Separator Size. Receiver separators are capable of separating up to 90% of the separator’s maximum flow-rate capacity and are used for heavy liquid loads or when footprint must be minimized. Most applications use a Standard design.
The “chosen size” is the next larger standard pipe size equal to or greater than the calculated requirement. Increase the chosen size if a lower differential pressure is required, then verify that the selected model’s separation capacity meets or exceeds the design liquid load.
Air and Other Vapors – required inputs:
NOTE: While design (maximum) pressure is required to determine the pressure class of the vessel, it is not required for separator sizing. Using the maximum possible temperature with the minimum possible pressure produces the “worst-case” gas volume for calculation purposes.
If both volumetric and mass flow values are available, convert mass flow to volumetric units and use the higher SCFM value. Mass flow is usually more accurate because it includes entrained liquid.
The >0.3 micron threshold corresponds to a single specialized model (TF). The >5 micron threshold is offered in three coalescing designs. All other designs satisfy the common >10 micron requirement.
When comparing models, pay attention to separation capacity and ability to handle liquid slugs. Each separator datasheet describes design, acceptable installation orientations, maximum separation capacity and slug-handling capability.
All fabricated designs can be customized. Common options include:
Standard documentation meets ASME Code Section VIII Division 1 requirements for code-stamped vessels (hydrostatic test confirmation and outline drawing). Additional documentation available when specified on the purchase order includes:
Most of the above documentation is provided for record only and carries an applicable cost. Many documents cannot be generated after fabrication, testing and code stamping are completed.
ASME Code Section VIII Division 1 provides the rules for design, fabrication, inspection, testing and certification of pressure vessels. Any non-standard NDE/NDT or documentation requirements must be communicated during the proposal stage so that we can confirm what can be provided and adjust pricing and lead time accordingly.
Use our website calculators to obtain a preliminary size, then contact us with your complete design criteria so we can prepare a detailed proposal.