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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…

Water Treating Equipment

Precipitators Coalescing Filters Process

Posted on September 5, 2009October 31, 2012

In the past, it was common to direct the water to be treated through a bed of excelsior or another similar medium, as shown in…

Basic Separation

Separating Oil, Water, and Gas with Weir System Separators

Posted on February 9, 2024

A weir system separator is a device that separates a mixture of oil, water, and gas into its individual components. It is commonly used in…

Treater Vessels Sizing

Treater Separator Settling Equations

Posted on September 15, 2009October 30, 2012

The specific gravity difference between the dispersed water droplets and the oil should result in the water “sinking” to the bottom of the treatment vessel.…

Two Phase Oil and Gas Separation

Maintain Optimum Pressure on Separator

Posted on December 13, 2021

For an oil and gas separator to accomplish its primary functions, pressure must be maintained in the separator so that the liquid and gas can…

Mechanical Design of Pressure Vessels

Pressure Vessels Ladder and Platform

Posted on September 24, 2009October 29, 2012

Vessel Supports Small vertical vessels may be supported by angle support legs, as shown in Figure 12-11. Larger vertical vessels are generally supported by a…

Gas Processing

Gas Stripping Service

Posted on May 27, 2013

For stripping service, as in a glycol or amine contactor , bubble cap trays are the most common. In recent years, there has been a…

Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

Treater Vessels Sizing

Treaters Separator Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine theĀ  diameter (d), length or height of the coalescing section (Leff or h),…

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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Recent Posts

  • Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs
  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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  • Two Phase Oil and Gas Separation
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  • Type Of Devices
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