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LTX Units and Line Heaters

LTX Unit Condensate Stabilizer

Posted on May 27, 2013

It should be clear from the description of LTX units that the lower pressure separator in an LTX unit is a simple form of cold-feed…

Relief Valve Sizing

Orifice Gas Flow Rate

Posted on September 25, 2009October 28, 2012

The flow rate for gas through a given orifice area or the area required  for a given flow rate is obtained by:

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…

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 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…

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…

Hydrates

Gas Expansion Temperature Drop

Posted on September 15, 2009October 30, 2012

Choking, or expansion of gas from a high pressure to a lower pressure, is generally required for control of gas flow rates. Choking is achieved…

Relief Valve Sizing

Liquids Flow Rate

Posted on September 25, 2009October 28, 2012

Conventional Valve, Balanced-Bellows Valve, or Pilot-Operated Valve The corresponding equations for liquid flow are the following: Note that a preliminary orifice size must be determined…

Shell and Tube Exchangers

Heat Exchanger Tube Pitch

Posted on September 13, 2009October 31, 2012

Tube holes cannot be drilled very close together, since this may structually weaken the tube sheet. The shortest distance between two adjacent tube holes is…

Mechanical Design of Pressure Vessels

Pressure Vessels Maximum Allowable Stress Values

Posted on September 23, 2009October 29, 2012

The maximum allowable stress values to be used in the calculation of the vessel’s wall thickness are given in the ASME Code for many different…

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Categories

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  • LTX Units and Line Heaters
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  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Two Phase Oil and Gas Separation
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  • Type Of Devices
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