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Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

Two Phase Separator Theory

Two Phase Separator Settling Time

Posted on September 14, 2009October 30, 2012

In the gravity settling section the liquid drops will settle at a velocity determined by equating the gravity force on the drop with the drag…

Heat Exchangers

Plate and Frame Exchangers

Posted on September 15, 2009October 29, 2012

Plate-and-frame exchangers are an arrangement of gasketed, pressed metal plates aligned on carrying bars and secured between two covers by compression bolts. The pressed metal…

Potential Operating Problem

Sand Problems

Posted on September 2, 2009

Sand can be very troublesome in separators by causing cutout of valve trim, plugging of separator internals, and accumulation in the bottom of the separator.…

Water Treating Equipment

Disposal Piles

Posted on September 5, 2009

Disposal piles are large diameter (24- to 48-inch) open-ended pipes attached to the platform and extending below the surface of the water. Their main uses…

Two Phase Oil and Gas Separation

Maintain Optimum Pressure on Separator

Posted on December 13, 2021

For an oil and gas separator to accomplish its primary functions, pressure must be maintained in the separator so that the liquid and gas can…

Crude Oil Treating System

Vertical Treaters Separator

Posted on September 2, 2009October 30, 2012

The most commonly used single-well lease treater is the vertical treater as shown in Figure 6-8. Flow enters the top of the treater into a…

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…

Water Treating Theory

Water Treating Coalescence

Posted on September 3, 2009

The process of coalescence in water treating systems is more time dependent than the process of dispersion. In dispersions of two immiscible liquids, immediate coalescence…

Shell and Tube Exchangers

Heat Exchanger Tubes

Posted on September 13, 2009October 31, 2012

Heat-exchanger tubes should not be confused with steel pipe or other types of pipe that are extruded to steel pipe sizes. The outside diameter of…

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Categories

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  • Fractions from atmospheric and vacuum distillation
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  • Type Of Devices
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