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Relief Valve Sizing

Effects of Back Pressure

Posted on September 25, 2009October 28, 2012

Back-pressure can affect either the set pressure or the capacity of a relief valve. The set pressure is the pressure at which the relief valve…

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…

Crude Oil Treating System

Coalescing Media

Posted on September 1, 2009

It is possible to use a coalescing media to promote coalescence of the water droplets. These media provide large surface area upon which water droplets…

Flotation Units

Dispersed Gas Units Separator

Posted on September 5, 2009October 29, 2012

In dispersed gas units gas bubbles are dispersed in the total stream either by the use of an inductor device or by a vortex set…

Water Treating Equipment

Corrugated Plate Interceptor Design

Posted on September 4, 2009October 31, 2012

The most common form of parallel plate interceptor used in oil facilities is the corrugated plate interceptor (CPI). This is a refinement of the PPI…

Fluid Properties

Liquid Flow Rate

Posted on September 16, 2009October 29, 2012

The liquid flow rate in moles per day for a given inlet stream can be determined from Equation 3-17. In our example, for an inlet…

Oil and Water Separation

Horizontal Three Phase Separator Part 2

Posted on August 21, 2009October 29, 2012

Figure 5-3 shows an alternate configuration known as a “bucket and weir” design. This design eliminates the need for a liquid interface controller. Both the…

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…

Two Phase Oil and Gas Separation

Double Barrel and Filter Separator

Posted on August 17, 2009October 30, 2012

Cyclone separators are designed to operate by centrifugal force. These designs are best suited for fairly clean gas streams. The swirling action of the gas…

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…

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Recent Posts

  • Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs
  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
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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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