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Pressure Drop in Piping

Moody Friction Factor

Posted on September 25, 2009October 28, 2012

The factor of proportionality in the previous equations is called the  Moody friction factor and is determined from the Moody resistance diagram shown in Figure…

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…

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…

Crude Oil Treating System

Crude Oil Treating System

Posted on August 23, 2009

Removing water from crude oil often requires additional processing beyond gravitational separation. In selecting a treating system, several factors should be considered to determine the…

Two Phase Oil and Gas Separation

Scrubbers Separator

Posted on August 17, 2009

A scrubber is a two-phase separator that is designed to recover liquids carried over from the gas outlets of production separators or to catch liquids…

Mechanical Design of Pressure Vessels

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

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…

Separation

Process Separator Operating Pressure

Posted on August 20, 2009October 31, 2012

The choice of separator operating pressures in a multistage system is large. For large facilities many options should be investigated before a final choice is…

Fluid Properties

The Flow Stream

Posted on September 16, 2009October 29, 2012

Many times the designer is given the mole fraction of each component in the feed stream but is not given the mole flow rate for…

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…

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Recent Posts

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  • Head Bernoulli Equation in Process Engineering
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