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Fractions from atmospheric and vacuum distillation

Naphthas

Posted on September 26, 2009October 28, 2012

There are usually two naphtha cuts produced from most crude. These are: Light naphtha (sometimes called light gasoline) Heavy naphtha. Both these streams are the…

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…

Two Phase Separator Equipment

Separator Mist Extractor

Posted on August 17, 2009October 28, 2012

Mist extractors can be made of wire mesh, vanes, centrifugal force devices, or packing. Wire mesh pads (Figure 4-10) are made of finely woven mats…

LTX Units and Line Heaters

Fire Tube Sizing

Posted on September 16, 2009October 28, 2012

The area of the fire tube is normally calculated based on a heat flux rate of 10,000 Btu/hr-ft2. The fire-tube length can be determined from:…

LTX Units and Line Heaters

LTX Wall Thickness Sizing

Posted on September 16, 2009October 28, 2012

Before choosing a wall thickness it is necessary to choose a pressure rating for the coil. Typically, the high-pressure coil (L1) is rated for the…

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…

Shell and Tube Exchangers

Heat Exchanger Types

Posted on September 14, 2009October 29, 2012

There are many different arrangements of the shells, tubes and baffles in heat exchangers. Figure 3-6 is a list of TEMA standard classifications for heat…

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…

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…

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…

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Categories

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  • Fractions from atmospheric and vacuum distillation
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  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • 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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  • Water Treating Theory
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