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Influent Water Quality

Soluble Oil

Posted on September 6, 2009

In every system substances that show up as “oil” in the laboratory test procedure will be dissolved in the water. This is especially true where…

Two Phase Separator Sizing

Two Phase Vertical Separators Sizing

Posted on September 14, 2009October 30, 2012

In vertical separators, a minimum diameter must be maintained to allow liquid drops to separate from the vertically moving gas. The liquid retention time requirement…

Two Phase Oil and Gas Separation

Scrubbers Separator

Posted on August 17, 2009

A scrubber is a two-phase separator that is designed to recover liquids carried over from the gas outlets of production separators or to catch liquids…

Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

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…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Shop Drawings

Posted on September 24, 2009October 29, 2012

Before the vessel fabrication can proceed, the fabricator will develop complete drawings and have these drawings approved by the representative of the engineering firm and/or…

Relief Valve Sizing

Critical Flow

Posted on September 25, 2009October 28, 2012

The flow of a compressible fluid through an orifice is limited by critical flow. Critical flow is also referred to as choked flow, sonic flow,…

Hydrates

Kinetic Inhibitor Process

Posted on September 15, 2009

A kinetic inhibitor is a polymeric chemical that, when added to a production stream, will not change the hydrate formation temperature but will delay the…

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…

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…

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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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  • Cyclone Separator Capacity

Categories

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  • Two Phase Separator Sizing
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  • Type Of Devices
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