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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

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

Production Process Component

Separator Level Control

Posted on August 20, 2009

It is also necessary to control the gas/liquid interface or the oil/water interface in process equipment. This is done with a level controller and liquid…

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.…

Separation

Processes of magnetic separation

Posted on December 27, 2021

When a magnetizable solid is subjected to a magnetic induction field, the local magnetic moments are oriented in the direction of the induction fields, and…

Two Phase Separator Sizing

Two Phase Vertical Separators Sizing

Posted on September 14, 2009October 30, 2012

In vertical separators, a minimum diameter must be maintained to allow liquid drops to separate from the vertically moving gas. The liquid retention time requirement…

Water Treating Equipment

Cross-Flow Separator

Posted on September 4, 2009October 31, 2012

Equipment manufacturers have modified the CPI configuration for horizontal water flow perpendicular to the axis of the corrugations in the plates as shown in Figure…

Gas Processing

SulfaTreat Process

Posted on May 27, 2013

SulfaTreat  process is similar to the iron sponge process. It uses a patented proprietary mixture of ferric oxide and triferric oxide to react with H2O…

Heat Exchangers

Aerial Coolers Part 1

Posted on September 15, 2009October 28, 2012

Aerial coolers are often used to cool a hot fluid to near ambient temperature. They are mechanically simple and flexible, and they eliminate the nuisance…

Mechanical Design of Pressure Vessels

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

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Recent Posts

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Categories

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  • Fractions from atmospheric and vacuum distillation
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  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
  • Produced Water Treating System
  • Production Process Component
  • Relief Valve Sizing
  • Separation
  • 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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