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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…

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…

Water Treating Theory

Gravity Separation Water Treating

Posted on September 2, 2009October 30, 2012

Most commonly used water treating equipment items rely on the forces of gravity to separate the oil droplets from the water continuous phase. The oil…

Oil and Water Separation

Horizontal Three Phase Separator Part 1

Posted on August 21, 2009October 31, 2012

Three phase separator are designed as either horizontal or vertical pressure vessel. Figure 5-2 is a schematic of a horizontal separator. The fluid enters the…

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…

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…

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…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

Hydrates

Gas Expansion Temperature Drop

Posted on September 15, 2009October 30, 2012

Choking, or expansion of gas from a high pressure to a lower pressure, is generally required for control of gas flow rates. Choking is achieved…

Flotation Units

Dissolved Gas Units Design

Posted on September 5, 2009October 31, 2012

Dissolved gas designs take a portion of the treated water effluent and saturate the water with natural gas in a contactor. The higher the pressure…

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Categories

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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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  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
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