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Separation

Stages Separation Selection

Posted on August 20, 2009October 29, 2012

As more stages are added to the process there is less and less incremental liquid recovery. The diminishing income for adding a stage must more…

Fractions from atmospheric and vacuum distillation

Vacuum Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the vacuum distillation unit. Just as in the case of the atmospheric residue it has several options for its…

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…

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…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Vortex Breaker and Manways

Posted on September 24, 2009October 28, 2012

Vortex Breaker As liquid flows out of the exit nozzle, it will swirl and create a vortex. Vortexing would carry the gas out with the…

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…

Production Process Component

Separator Control Valve

Posted on August 20, 2009October 30, 2012

Control valves are used throughout the process to control pressure, level, temperature, or flow. It is beyond the scope of this text to discussthe differences…

Fractions from atmospheric and vacuum distillation

Atmospheric Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the atmospheric distillation of the crude oil. Most crude oils are distilled in the atmospheric crude oil tower to…

Pressure Relief

Relief Valve Installation

Posted on September 25, 2009

Each relief valve should be equipped with inlet piping no smaller than the valve inlet flange size, and inlet piping should be as short as…

Mechanical Design of Pressure Vessels

Estimating Pressure Vessels Weights

Posted on September 23, 2009October 29, 2012

It is important to be able to estimate vessel weights, since most cost estimating procedures start with the weight of the vessel. The vessel weight,…

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Categories

  • Article
  • Basic Configuration
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  • Fractions from atmospheric and vacuum distillation
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  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Production Process Component
  • Relief Valve Sizing
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  • Separation
  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
  • Two Phase Separator Equipment
  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
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  • Water Treating Theory
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