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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…

Fluid Properties

Molecular Weight of Gas

Posted on September 16, 2009October 29, 2012

The molecular weight of the stream is calculated from the weighted average gas molecular weight given by: The molecular weight of the gas stream of…

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…

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…

Production Process Component

Separation Temperature Control

Posted on August 20, 2009

The way in which the process temperature is controlled varies. In a heater, a temperature controller measures the process temperature and signals a fuel valve…

Heat Exchangers

Fired Heater Design

Posted on September 15, 2009October 29, 2012

Direct-fired combustion equipment is that in which the flame and/or products of combustion are used to achieve the desired result by radiation and convection. Common…

Condensate Stabilization

Multistages Separation

Posted on September 16, 2009October 28, 2012

Figure 6-1 shows a multistage separation process. By removing molecules of the light components in the first separator they are not available to flash to…

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…

Heat Exchangers

Heat Recovery Unit

Posted on September 15, 2009

In the interest of energy conversion, process heat can be obtained from a heat recovery unit in which heat is recovered from turbine or reciprocating…

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…

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Categories

  • Article
  • Basic Configuration
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  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
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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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