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Potential Operating Problem

Foamy Crudes Problems

Posted on September 2, 2009

The major cause of foam in crude oil is the appearance of impurities, other than water, which are impractical to remove before the stream reaches…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Specifications

Posted on September 24, 2009October 29, 2012

Most companies have a detailed general specification for the construction of pressure vessels, which defines the overall quality of fabrication required and addresses specific items…

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…

Separation

Stages Separation Selection

Posted on August 20, 2009October 29, 2012

As more stages are added to the process there is less and less incremental liquid recovery. The diminishing income for adding a stage must more…

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…

Separation

Processes of magnetic separation

Posted on December 27, 2021

When a magnetizable solid is subjected to a magnetic induction field, the local magnetic moments are oriented in the direction of the induction fields, and…

Heat Exchangers

Aerial Coolers Basic Principle Part 2

Posted on September 15, 2009October 28, 2012

Process outlet temperature in an aerial cooler can be controlled by louvers, fan variable speed drives, blade pitch or recirculation of process fluid. As the…

Fractions from atmospheric and vacuum distillation

Straight Run Kerosene

Posted on September 26, 2009

This fraction is usually the first side stream of a conventional atmospheric distillation unit. It may be cut to meet a burning oil specification or…

Shell and Tube Exchangers

Heat Exchangers Classification

Posted on September 14, 2009

In addition to the type description code there is also a shorthand that is used for classifying heat exchangers. The first element of the shorthand…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

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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
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
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  • Heat Transfer Theory
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  • 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
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  • Relief Valve Sizing
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  • 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
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  • Water Treating Theory
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