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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…

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…

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,…

Basic Configuration

Lease Automatic Custudy Transfer

Posted on August 21, 2009October 29, 2012

In large facilities oil is typically sold through a LACT unit, which is designed to meet API Standards and whatever additional measuring and sampling standards…

Influent Water Quality

Deck Drainage

Posted on September 6, 2009

Federal regulations and most authorities having jurisdiction require that “free oil” be removed from deck drainage prior to disposal. It is extremely difficult to predict…

Treater Vessels Sizing

Treater Separator Retention Time Equations

Posted on September 15, 2009October 30, 2012

The oil must be held at temperature for a specific period of time to enable de-emulsifying the water-in-oil emulsion. This information is best determined in…

Mechanical Design of Pressure Vessels

Pressure Vessels Relief Devices and Corrosion Protection

Posted on September 24, 2009

Pressure Relief Devices All pressure vessels should be equipped with one or more pressure safety valves (PSVs) to prevent overpressure. This is a requirement of…

Separation

Intensity of magnetization and magnetic separation

Posted on December 27, 2021

When subjected to a magnetic induction B, an elementary volume v of magnetizable substance acquires local magnetization M, where M is the magnetic moment of…

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…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

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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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