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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…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Vortex Breaker and Manways

Posted on September 24, 2009October 28, 2012

Vortex Breaker As liquid flows out of the exit nozzle, it will swirl and create a vortex. Vortexing would carry the gas out with the…

Basic Separation

Separating Oil, Water, and Gas with Weir System Separators

Posted on February 9, 2024

A weir system separator is a device that separates a mixture of oil, water, and gas into its individual components. It is commonly used in…

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…

Gas Processing

Structured Packing

Posted on May 27, 2013May 27, 2013

A bed of structured packing consists of a bed support upon which elements of structured packing are placed. Beds of structured packing typically have lower…

Shell and Tube Exchangers

Heat Exchangers Classification

Posted on September 14, 2009

In addition to the type description code there is also a shorthand that is used for classifying heat exchangers. The first element of the shorthand…

Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

Two Phase Separator Theory

Two Phase Separator Retention Time

Posted on September 14, 2009

To assure that the liquid and gas reach equilibrium at separator pressure a certain liquid storage is required. This is defined as “retention time” or…

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…

Produced Water Treating System

Water Treating Processes

Posted on September 2, 2009

In producing operations it is often necessary to handle waste water that may include water produced with crude oil, rain water, and washdown water. The…

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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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