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Oil and Water Separation

Vertical Three Phase Separator Configuration

Posted on September 2, 2009October 29, 2012

Figure 5-6 shows a typical configuration for a vertical three-phase separator. Flow enters the vessel through the side as in the horizontal separator, the inlet…

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…

Separation

Intensity of magnetization and magnetic separation

Posted on December 27, 2021

When subjected to a magnetic induction B, an elementary volume v of magnetizable substance acquires local magnetization M, where M is the magnetic moment of…

Potential Operating Problem

Liquid Carryover and Gas Blowby

Posted on September 2, 2009

Liquid carryover and gas blowby are two common operating problems. Liquid carryover occurs when free liquid escapes with the gas phase and can indicate high…

Shell and Tube Exchangers

Heat Exchanger Tube Pitch

Posted on September 13, 2009October 31, 2012

Tube holes cannot be drilled very close together, since this may structually weaken the tube sheet. The shortest distance between two adjacent tube holes is…

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…

Fluid Properties

Gas Flow Rate

Posted on September 16, 2009October 29, 2012

If the flow rate of the inlet stream is known in moles per day then the number of moles per day of gas flow can…

Hydrates

Hydrate Formation Temperature or Pressure Determination

Posted on September 15, 2009October 28, 2012

Knowledge of the temperature and pressure of a gas stream at the wellhead is important for determining whether hydrate formation can be expected when the…

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…

Water Treating Equipment

Parallel Plate Interceptor Design

Posted on September 4, 2009October 29, 2012

The first form of a plate coalescer was the parallel plate interceptor (PPI). This involved installing a series of plates parallel to the longitudinal axis…

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Categories

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  • Two Phase Oil and Gas Separation
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  • Type Of Devices
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