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Two Phase Separator Equipment

Defoaming Plates Separator

Posted on August 17, 2009October 30, 2012

Foam at the interface may occur when gas bubbles are liberated from the liquid. This foam can be stabilized with the addition of chemicals at…

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…

Gas Processing

Physical Solvent Processes

Posted on August 20, 2020October 6, 2020

These processes are based on the solubility of the H2S and/or CO2 within the solvent, instead of on chemical reactions between the acid gas and…

Crude Oil Treating System

Gravity Separation Process

Posted on August 31, 2009October 30, 2012

Most oil-treating equipment relies on gravity to separate water droplets from the oil continuous phase, because water droplets are heavier than the volume of oil…

Type Of Devices

Balanced Bellows Relief Valves

Posted on September 25, 2009October 28, 2012

Balanced relief valves are spring-loaded valves that contain a bellows arrangement to keep back-pressure from affecting the set point. Figure 13-4 shows a cross section…

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…

Pressure Relief

Relief Header Design

Posted on September 25, 2009October 28, 2012

The relief header is a system of piping connecting the outlets of all the relief valves into a common pipe or header that goes to…

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…

Production Process Component

Separator Level Control

Posted on August 20, 2009

It is also necessary to control the gas/liquid interface or the oil/water interface in process equipment. This is done with a level controller and liquid…

Flotation Units

Dispersed Gas Units Sizing

Posted on September 5, 2009

It can be shown mathematically that an efficient design must have a high gas induction rate, a small diameter induced gas bubble, and relatively large…

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