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Shell and Tube Exchangers

TEMA Glasses and Tube Materials

Posted on September 15, 2009October 29, 2012

TEMA standards provide for two classes of shell and tube exchanger qualities. Class C is the lessĀ  stringent and is typically used in onshore applications…

LTX Units and Line Heaters

LTX Units

Posted on September 15, 2009October 28, 2012

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug…

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…

Crude Oil Treating System

Crude Oil Viscosity

Posted on September 1, 2009October 29, 2012

Laboratory testing of a particular oil at various temperatures is the most reliable method of determining how an oil behaves. ASTM D 341 outlines a…

Flotation Units

Dispersed Gas Units Separator

Posted on September 5, 2009October 29, 2012

In dispersed gas units gas bubbles are dispersed in the total stream either by the use of an inductor device or by a vortex set…

Water Treating Theory

Water Treating Flotation

Posted on September 3, 2009

The process of flotation improves the separation of the oil droplets from the water continuous phase. This goal is accomplished by increasing the difference in…

Condensate Stabilization

Multistages Separation

Posted on September 16, 2009October 28, 2012

Figure 6-1 shows a multistage separation process. By removing molecules of the light components in the first separator they are not available to flash to…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Inspection Procedures

Posted on September 23, 2009

All ASME Code vessels are inspected by an approved Code inspector. The manufacturer will supply Code papers signed by the inspector. The nameplate on the…

Pressure Relief

Relief Valve Installation

Posted on September 25, 2009

Each relief valve should be equipped with inlet piping no smaller than the valve inlet flange size, and inlet piping should be as short as…

Fractions from atmospheric and vacuum distillation

Vacuum Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the vacuum distillation unit. Just as in the case of the atmospheric residue it has several options for its…

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Recent Posts

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Categories

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  • Three Phase Separator Sizing
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  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
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  • Water Treating Theory
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