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Separation

Separator Initial Pressure

Posted on August 20, 2009October 31, 2012

Because of the multicomponent nature of the produced fluid, the higher the pressure at which the initial separation occurs, the more liquid will be obtained…

Fractions from atmospheric and vacuum distillation

Vacuum Distillation of Atmospheric Residue

Posted on September 26, 2009October 28, 2012

In modern refinery practice the distillation of atmospheric residue is accomplished under high vacuum conditions in a specially designed tower whose internal equipment ensures a…

Separation

Separation Stages

Posted on August 20, 2009October 28, 2012

Figure 2-5 deals with a simple single-stage process. That is, the fluids are flashed in an initial separator and then the liquids from that separator…

Shell and Tube Exchangers

TEMA Glasses and Tube Materials

Posted on September 15, 2009October 29, 2012

TEMA standards provide for two classes of shell and tube exchanger qualities. Class C is the lessĀ  stringent and is typically used in onshore applications…

Fluid Properties

Liquid Flow Rate

Posted on September 16, 2009October 29, 2012

The liquid flow rate in moles per day for a given inlet stream can be determined from Equation 3-17. In our example, for an inlet…

Gas Processing

Sulfinol Process

Posted on September 10, 2020October 6, 2020

Licensed by Shell the SulfinolĀ® process combines the properties of a physical and a chemical solvent. The Sulfinol solution consists of a mixture of sulfolane…

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,…

LTX Units and Line Heaters

LTX Coil Diameter Sizing

Posted on September 16, 2009October 28, 2012

Erosional flow criteria will almost always govern in choosing the diameter. Sometimes it is necessary to check for pressure drop in the coil. Typically, pressure…

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…

Heat Exchangers

Plate and Frame Exchangers

Posted on September 15, 2009October 29, 2012

Plate-and-frame exchangers are an arrangement of gasketed, pressed metal plates aligned on carrying bars and secured between two covers by compression bolts. The pressed metal…

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Categories

  • Article
  • Basic Configuration
  • Basic Separation
  • Condensate Stabilization
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  • Equations
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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
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  • Heat Transfer Theory
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  • Influent Water Quality
  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • 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
  • Water Treating Equipment
  • Water Treating Theory
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