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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.…

Mechanical Design of Pressure Vessels

Determining Separator Pressure Vessels Wall Thickness

Posted on September 23, 2009October 29, 2012

The following formulas are used in the ASME Code Section VIII, Division 1 for determining wall thickness: Wall thickness—cylindrical shells Figure 12-1 defines the various…

Potential Operating Problem

Liquid Carryover and Gas Blowby

Posted on September 2, 2009

Liquid carryover and gas blowby are two common operating problems. Liquid carryover occurs when free liquid escapes with the gas phase and can indicate high…

Potential Operating Problem

Paraffin Problems

Posted on September 2, 2009

Separator operation can be adversely affected by an accumulation of paraffin. Coalescing plates in the liquid section and mesh pad mist extractors in the gas…

Oil and Water Separation

Horizontal Three Phase Separator Part 2

Posted on August 21, 2009October 29, 2012

Figure 5-3 shows an alternate configuration known as a “bucket and weir” design. This design eliminates the need for a liquid interface controller. Both the…

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…

Pressure Relief

Relief Header Design

Posted on September 25, 2009October 28, 2012

The relief header is a system of piping connecting the outlets of all the relief valves into a common pipe or header that goes to…

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…

Water Treating Equipment

Corrugated Plate Interceptor Design

Posted on September 4, 2009October 31, 2012

The most common form of parallel plate interceptor used in oil facilities is the corrugated plate interceptor (CPI). This is a refinement of the PPI…

Gas Processing

Gas Sweetening Processes

Posted on May 27, 2013

Numerous processes have been developed for gas sweetening based on a variety of chemical and physical principles. These processes can be categorized by the principles…

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Recent Posts

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  • Head Bernoulli Equation in Process Engineering
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Categories

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  • Fractions from atmospheric and vacuum distillation
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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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  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • 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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