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Fluid Properties

Liquid Molecular Weight Calculation

Posted on September 16, 2009October 29, 2012

The molecular weight of the liquid stream is calculated from the weighted average liquid component molecular weight given by: This is calculated in Table 3-3.…

Pressure Relief

Process Relief Requirements

Posted on September 25, 2009

The ASME code requires every pressure vessel that can be blocked In to have a relief valve to alleviate pressure build up due to thermal…

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…

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…

Production Process Component

Separation Flow Control

Posted on August 20, 2009

It is very rare that flow must be controlled in an oil field process. Normally, the control of pressure, level, and temperature is sufficient. Occasionally,…

Shell and Tube Exchangers

Heat Exchanger Baffles

Posted on September 13, 2009October 31, 2012

Shell-and-tube exchangers contain several types of baffles to help direct the flow of both tube-side and shell-side fluids. Pass partition baffles force the fluid to…

Fractions from atmospheric and vacuum distillation

Atmospheric Overhead Distillate

Posted on September 26, 2009October 28, 2012

This is not strictly a cut but consists of all the light material in the crude absorbed into the total overhead distillate from the crude…

Pressure Drop in Piping

Reynolds Number Piping

Posted on September 25, 2009October 28, 2012

The Reynolds number is a dimensionless parameter that relates the ratio of inertial forces to viscous forces. It can be expressed by the following general…

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…

Shell and Tube Exchangers

Heat Exchanger Placement of Fluid

Posted on September 14, 2009

The question always comes up of which fluid to put in the tubes and which fluid to put in the shell. Consider placing a fluid…

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Recent Posts

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Categories

  • Article
  • Basic Configuration
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  • Equations
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  • 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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