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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…

Shell and Tube Exchangers

Shell and Tube Exchangers

Posted on September 13, 2009October 31, 2012

Shell-and-tube heat exchangers are cylindrical in shape, consisting of a bundle of parallel tubes surrounded by an outer casing (shell). Both the tube bundle and…

Two Phase Separator Equipment

Wave Breakers

Posted on August 17, 2009

In long horizontal vessels it is necessary to install wave breakers, which are nothing more than vertical baffles spanning the gas-liquid interface and perpendicular to…

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…

Gas Processing

Physical Solvent Processes

Posted on August 20, 2020October 6, 2020

These processes are based on the solubility of the H2S and/or CO2 within the solvent, instead of on chemical reactions between the acid gas and…

Oil and Water Separation

Vertical Three Phase Separator Configuration

Posted on September 2, 2009October 29, 2012

Figure 5-6 shows a typical configuration for a vertical three-phase separator. Flow enters the vessel through the side as in the horizontal separator, the inlet…

Pressure Relief

Pressure Relief Valves

Posted on September 25, 2009

The most important safety devices in a production facility are the pressure relief valves, which ensure that pipes, valves, fittings, and pressure vessels can never…

Production Process Component

Separation Temperature Control

Posted on August 20, 2009

The way in which the process temperature is controlled varies. In a heater, a temperature controller measures the process temperature and signals a fuel valve…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Nozzles

Posted on September 24, 2009October 29, 2012

Nozzles should be sized according to pipe sizing criteria, such as those provided in API RP 14E. The outlet nozzle is generally the same size…

Treater Vessels Sizing

Treater Separator Settling Equations

Posted on September 15, 2009October 30, 2012

The specific gravity difference between the dispersed water droplets and the oil should result in the water “sinking” to the bottom of the treatment vessel.…

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Recent Posts

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  • Cyclone Separator Capacity

Categories

  • Article
  • Basic Configuration
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  • 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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