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Basic Separation

Horizontal Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

Separators are designed in either horizontal, vertical, or spherical configurations. Figure 4-1 is a schematic of a horizontal separator. The initial gross separation of liquid…

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…

Pressure Drop in Piping

Bernoulli’s Theorem

Posted on September 25, 2009October 28, 2012

It is customary to express the energy contained in a fluid in terms of the potential energy contained in an equivalent height or “head” of…

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…

Water Treating Equipment

Hydrocyclone Separator

Posted on January 6, 2011October 28, 2012

Hydrocyclone separators, sometimes called enhanced gravity separators, use centrifugal force to remove oil droplets from oily water. As shown in Figure 7-16, static hydrocyclone separator…

Two Phase Separator Sizing

Two Phase Horizontal Separators Sizing

Posted on September 14, 2009October 30, 2012

For sizing a horizontal separator it is necessary to choose a seam-toseam  vessel length and a diameter. This choice must satisfy the conditions  for gas…

Shell and Tube Exchangers

Shell and Tube Heat Exchanger Sizing

Posted on September 15, 2009October 29, 2012

The required heat duty, film coefficients, conductivity, etc. for a shell and tube heat exchanger can be calculated using the procedures in Heat Transfer Theory,…

Gas Processing

Gas Sweetening Processes

Posted on May 27, 2013

Numerous processes have been developed for gas sweetening based on a variety of chemical and physical principles. These processes can be categorized by the principles…

Water Treating Theory

Water Treating Dispersion

Posted on September 3, 2009October 28, 2012

An oscillating droplet of oil becomes unstable when the kinetic energy is sufficient to make up for the difference in the surface energy between the…

Two Phase Oil and Gas Separation

INTERNAL CONSTRUCTION OF SEPARATORS

Posted on December 13, 2021December 13, 2021

The principal items of construction that should be present in a good liquid-gas separator are the same regardless of the over-al1 shape or configuration of…

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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
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
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  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • 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
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  • Water Treating Theory
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