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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…

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…

Fractions from atmospheric and vacuum distillation

Atmospheric Overhead Distillate

Posted on September 26, 2009October 28, 2012

This is not strictly a cut but consists of all the light material in the crude absorbed into the total overhead distillate from the crude…

Separation

Processes of magnetic separation

Posted on December 27, 2021

When a magnetizable solid is subjected to a magnetic induction field, the local magnetic moments are oriented in the direction of the induction fields, and…

Gas Processing

Gas Dehydration Method

Posted on May 23, 2013

Contactor column usually contain either tray random packing or structure packing. For large volume of gas, the contactor is usually a tray column consisting of…

Basic Configuration

Oil Treating Process

Posted on August 21, 2009October 31, 2012

Most oil treating on offshore facilities is done in vertical or horizontal treaters, such as those described in “Crude Oil Treating System“. Figure 2-8 is…

Fluid Properties

Specific Gravity and Density

Posted on September 16, 2009October 29, 2012

Specific gravity of a liquid is the ratio of the density of the liquid at 60°F to the density of pure water. API gravity is…

Type Of Devices

Pilot Operated Relief Valves

Posted on September 25, 2009October 28, 2012

Pilot-operated relief valves use the pressure in the vessel rather than a spring to seal the valve and a pilot to activate the mechanism. Figure…

Hydrates

Hydrate Formation Temperature or Pressure Determination

Posted on September 15, 2009October 28, 2012

Knowledge of the temperature and pressure of a gas stream at the wellhead is important for determining whether hydrate formation can be expected when the…

Crude Oil Treating System

Oil Treating Systems Coalescence

Posted on September 1, 2009October 30, 2012

The process of coalescence in oil treating systems is time dependent. In dispersions of two immiscible liquids, immediate coalescence seldom occurs when two droplets collide.…

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Recent Posts

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Categories

  • Article
  • Basic Configuration
  • Basic Separation
  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
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  • Fluid Properties
  • 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
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  • 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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