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Oil and Water Separation

Vessel Internal Design

Posted on September 2, 2009

Two common internals not discussed are coalescing plates and sand jets. It is possible to use various plate or pipe coalescer designs to aid in…

Heat Exchangers

Heat Recovery Unit

Posted on September 15, 2009

In the interest of energy conversion, process heat can be obtained from a heat recovery unit in which heat is recovered from turbine or reciprocating…

Shell and Tube Exchangers

Shell and Tube Exchangers

Posted on September 13, 2009October 31, 2012

Shell-and-tube heat exchangers are cylindrical in shape, consisting of a bundle of parallel tubes surrounded by an outer casing (shell). Both the tube bundle and…

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,…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Inspection Procedures

Posted on September 23, 2009

All ASME Code vessels are inspected by an approved Code inspector. The manufacturer will supply Code papers signed by the inspector. The nameplate on the…

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…

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…

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…

Mechanical Design of Pressure Vessels

Determining Separator Pressure Vessels Wall Thickness

Posted on September 23, 2009October 29, 2012

The following formulas are used in the ASME Code Section VIII, Division 1 for determining wall thickness: Wall thickness—cylindrical shells Figure 12-1 defines the various…

Two Phase Separator Theory

Two Phase Separator Drop Size

Posted on September 14, 2009

The purpose of the gas separation section of the vessel is to condition the gas for final polishing by the mist extractor. From field experience…

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Categories

  • Article
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  • Fractions from atmospheric and vacuum distillation
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  • Oil and Water Separation
  • Potential Operating Problem
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  • Pressure Relief
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  • 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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