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Gas Processing

Gas Stripping Service

Posted on May 27, 2013

For stripping service, as in a glycol or amine contactor , bubble cap trays are the most common. In recent years, there has been a…

Shell and Tube Exchangers

Heat Exchanger Selections

Posted on September 14, 2009October 31, 2012

In selecting an exchanger, one must know the advantages and disadvantages of each type. The three basic types of shell-and-tube exchangers are fixed tube sheet,…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

Fluid Properties

Liquid Specific Gravity

Posted on September 16, 2009October 29, 2012

Remembering that the weight of each component is the number of moles of that component times its molecular weight (pounds = MW X moles), the…

Crude Oil Treating System

Oil Treating Systems Coalescence

Posted on September 1, 2009October 30, 2012

The process of coalescence in oil treating systems is time dependent. In dispersions of two immiscible liquids, immediate coalescence seldom occurs when two droplets collide.…

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…

Water Treating Equipment

Hydrocyclone Separator

Posted on January 6, 2011October 28, 2012

Hydrocyclone separators, sometimes called enhanced gravity separators, use centrifugal force to remove oil droplets from oily water. As shown in Figure 7-16, static hydrocyclone separator…

Fluid Properties

Gas Flow Rate

Posted on September 16, 2009October 29, 2012

If the flow rate of the inlet stream is known in moles per day then the number of moles per day of gas flow can…

LTX Units and Line Heaters

Line Heaters

Posted on September 15, 2009October 30, 2012

As shown in Figure 5-2, the well stream enters the first coil at its flowing tubing temperature and pressure. Alternatively, it could be choked at…

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…

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Recent Posts

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