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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…

Relief Valve Sizing

Two-Phase Flow Standard Sizes

Posted on September 25, 2009October 28, 2012

Two-Phase Flow There are no precise formulas for calculating orifice area for twophase flow. The common convention is to calculate the area required for the…

LTX Units and Line Heaters

LTX Coil Lengths Sizing

Posted on September 16, 2009October 28, 2012

With the known temperatures on each end of the coil, the heat duty for each coil can be calculated from the heat transfer theory. Since…

Fractions from atmospheric and vacuum distillation

Atmospheric Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the atmospheric distillation of the crude oil. Most crude oils are distilled in the atmospheric crude oil tower to…

Pressure Relief

Relief Valve Vent or Flare Tip

Posted on September 25, 2009

A pipe that releases gas to disperse into the atmosphere is called a vent. If the gas is burned at the tip, it is called…

Potential Operating Problem

Paraffin Problems

Posted on September 2, 2009

Separator operation can be adversely affected by an accumulation of paraffin. Coalescing plates in the liquid section and mesh pad mist extractors in the gas…

Two Phase Oil and Gas Separation

Spherical Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

A typical spherical separator is shown in Figure 4-3. The same four sections can be found in this vessel. Spherical separators are a special case…

Gas Processing

Tray Efficiency and Tower Height

Posted on May 27, 2013

In condensate stabilizers, trays generally have 70% equilibrium stage efficiency. That is, 1.4 actual trays are required to provide one theoretical stage. The spacing between…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Inspection Procedures

Posted on September 23, 2009

All ASME Code vessels are inspected by an approved Code inspector. The manufacturer will supply Code papers signed by the inspector. The nameplate on the…

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Recent Posts

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Categories

  • Article
  • Basic Configuration
  • Basic Separation
  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
  • Flotation Units
  • 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
  • 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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