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Crude Oil Treating System

Electrostatic Treaters Process

Posted on September 2, 2009October 30, 2012

Some treaters use an electrode section. Figure 6-11 illustrates a typical design of a horizontal electrostatic treater. The flow path in an electrostatic treater is…

LTX Units and Line Heaters

LTX Units

Posted on September 15, 2009October 28, 2012

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug…

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…

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

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

Water Treating Theory

Water Treating Flotation

Posted on September 3, 2009

The process of flotation improves the separation of the oil droplets from the water continuous phase. This goal is accomplished by increasing the difference in…

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…

Mechanical Design of Pressure Vessels

Pressure Vessels Relief Devices and Corrosion Protection

Posted on September 24, 2009

Pressure Relief Devices All pressure vessels should be equipped with one or more pressure safety valves (PSVs) to prevent overpressure. This is a requirement of…

Type Of Devices

Rupture Discs

Posted on September 25, 2009

These are thin diaphragms held between flanges and calibrated to burst at a specified static inlet pressure. Unlike relief valves, rapture discs cannot reseal when…

Two Phase Separator Theory

Two Phase Separator Retention Time

Posted on September 14, 2009

To assure that the liquid and gas reach equilibrium at separator pressure a certain liquid storage is required. This is defined as “retention time” or…

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Recent Posts

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  • Head Bernoulli Equation in Process Engineering
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  • Cyclone Separator Capacity

Categories

  • Article
  • Basic Configuration
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  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
  • Flotation Units
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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
  • Heat Exchangers
  • Heat Transfer Theory
  • Hydrates
  • Influent Water Quality
  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
  • Produced Water Treating System
  • Production Process Component
  • Relief Valve Sizing
  • Separation
  • Separation
  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
  • Two Phase Separator Equipment
  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
  • Water Treating Equipment
  • Water Treating Theory
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