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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…

Three Phase Separator Sizing

Three Phase Vertical Separators Sizing

Posted on September 14, 2009October 30, 2012

As with vertical two-phase separators, a minimum diameter must be  maintained to assure adequate gas capacity. In addition, vertical threephase  separators must maintain a minimum…

Crude Oil Treating System

Gravity Separation Process

Posted on August 31, 2009October 30, 2012

Most oil-treating equipment relies on gravity to separate water droplets from the oil continuous phase, because water droplets are heavier than the volume of oil…

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…

Basic Configuration

Lease Automatic Custudy Transfer

Posted on August 21, 2009October 29, 2012

In large facilities oil is typically sold through a LACT unit, which is designed to meet API Standards and whatever additional measuring and sampling standards…

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…

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.…

Type Of Devices

Balanced Bellows Relief Valves

Posted on September 25, 2009October 28, 2012

Balanced relief valves are spring-loaded valves that contain a bellows arrangement to keep back-pressure from affecting the set point. Figure 13-4 shows a cross section…

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.…

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…

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Categories

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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
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  • Two Phase Separator Sizing
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  • Type Of Devices
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