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Two Phase Oil and Gas Separation

Maintain Liquid Seal in Separator

Posted on December 13, 2021

To maintain pressure on a separator, a liquid seal must be effected in the lower portion of the vessel. This liquid seal prevents loss of…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

Crude Oil Treating System

Electrostatic Coalescers Process

Posted on September 1, 2009October 29, 2012

Coalescing of the small water drops dispersed in the crude can be accomplished by subjecting the water-in-oil emulsion to a high-voltage electrical field. When a…

Two Phase Oil and Gas Separation

Vertical Two Phase Separator Basic Design

Posted on August 17, 2009October 29, 2012

Figure 4-2 is a schematic of a vertical separator. In this configuration the inlet flow enters the vessel through the side. As in the horizontal…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

Pressure Drop in Piping

Pressure Drop In Piping

Posted on September 25, 2009

Piping design in production facilities involves the selection of a pipe diameter and a wall thickness that is capable of transporting fluid from one piece…

Production Process Component

Separation Flow Control

Posted on August 20, 2009

It is very rare that flow must be controlled in an oil field process. Normally, the control of pressure, level, and temperature is sufficient. Occasionally,…

Crude Oil Treating System

Emulsifying Agent

Posted on August 30, 2009

When thinking about emulsion stability, it may be helpful to realize that in a pure oil and pure water mixture, without an emulsifying agent, no…

Crude Oil Treating System

Forming Emulsions Process

Posted on August 23, 2009October 31, 2012

For an emulsion to exist there must be two mutually immiscible liquids, an emulsifying agent, and sufficient agitation to disperse the discontinuous phase into the…

Gas Processing

Tray Efficiency and Tower Height

Posted on May 27, 2013

In condensate stabilizers, trays generally have 70% equilibrium stage efficiency. That is, 1.4 actual trays are required to provide one theoretical stage. The spacing between…

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