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Flotation Units

Dispersed Gas Units Separator

Posted on September 5, 2009October 29, 2012

In dispersed gas units gas bubbles are dispersed in the total stream either by the use of an inductor device or by a vortex set…

Treater Vessels Sizing

Treaters Water Separator Droplet Size

Posted on September 15, 2009October 30, 2012

In order to develop a treater design procedure, the water droplet size to be used in the settling equation to achieve a given outlet water…

Water Treating Equipment

Skim Pile

Posted on September 5, 2009October 31, 2012

The skim pile is a type of disposal pile. As shown in Figure 7-18, flow through the multiple series of baffle plates creates zones of…

Mechanical Design of Pressure Vessels

Estimating Pressure Vessels Weights

Posted on September 23, 2009October 29, 2012

It is important to be able to estimate vessel weights, since most cost estimating procedures start with the weight of the vessel. The vessel weight,…

Influent Water Quality

Water Treating System Produced Water

Posted on September 5, 2009October 31, 2012

The first step in choosing a water treating system is to characterize the influent water streams. It is necessary to know both the oil concentration…

Two Phase Oil and Gas Separation

Maintain Liquid Seal in Separator

Posted on December 13, 2021

To maintain pressure on a separator, a liquid seal must be effected in the lower portion of the vessel. This liquid seal prevents loss of…

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…

Fluid Properties

Liquid Specific Gravity

Posted on September 16, 2009October 29, 2012

Remembering that the weight of each component is the number of moles of that component times its molecular weight (pounds = MW X moles), the…

Three Phase Separator Sizing

Three Phase Horizontal Separator Sizing

Posted on September 14, 2009October 30, 2012

For sizing a horizontal three-phase separator it is necessary to specify a vessel diameter and a seam-to-seam vessel length. The gas capacity and retention time…

Relief Valve Sizing

Orifice Gas Flow Rate

Posted on September 25, 2009October 28, 2012

The flow rate for gas through a given orifice area or the area required  for a given flow rate is obtained by:

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Categories

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  • Potential Operating Problem
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  • Pressure Relief
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  • 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
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  • Type Of Devices
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