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Crude Oil Treating System

Water Droplet Size and Retention Time

Posted on September 1, 2009

The droplet diameter is the most important single parameter to control to aid in water settling since this term is squared in the settling equation.…

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…

Hydrates

Kinetic Inhibitor Process

Posted on September 15, 2009

A kinetic inhibitor is a polymeric chemical that, when added to a production stream, will not change the hydrate formation temperature but will delay the…

Shell and Tube Exchangers

Heat Exchanger Types

Posted on September 14, 2009October 29, 2012

There are many different arrangements of the shells, tubes and baffles in heat exchangers. Figure 3-6 is a list of TEMA standard classifications for heat…

Treater Vessels Sizing

Treaters Separator Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine the  diameter (d), length or height of the coalescing section (Leff or h),…

Heat Transfer Theory

Oil Sensible Heat Duty

Posted on September 13, 2009October 29, 2012

The sensible heat duty for the oil phase is: where Q0 = oil flow rate, bpd SG = oil specific gravity C0 = oil specific…

Heat Exchangers

Aerial Coolers Part 1

Posted on September 15, 2009October 28, 2012

Aerial coolers are often used to cool a hot fluid to near ambient temperature. They are mechanically simple and flexible, and they eliminate the nuisance…

Crude Oil Treating System

Emulsifying Agent

Posted on August 30, 2009

When thinking about emulsion stability, it may be helpful to realize that in a pure oil and pure water mixture, without an emulsifying agent, no…

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.…

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…

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Categories

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  • Type Of Devices
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