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Relief Valve Sizing

Two-Phase Flow Standard Sizes

Posted on September 25, 2009October 28, 2012

Two-Phase Flow There are no precise formulas for calculating orifice area for twophase flow. The common convention is to calculate the area required for the…

Gas Processing

Gas Dehydration Method

Posted on May 23, 2013

Contactor column usually contain either tray random packing or structure packing. For large volume of gas, the contactor is usually a tray column consisting of…

Gas Processing

Acid Gas Treating Process

Posted on May 27, 2013May 27, 2013

Next to sales contract specifications, corrosion protection ranks highest among the reasons for the removal of acid gases. The partial pressure of the acid gases…

Fractions from atmospheric and vacuum distillation

Naphthas

Posted on September 26, 2009October 28, 2012

There are usually two naphtha cuts produced from most crude. These are: Light naphtha (sometimes called light gasoline) Heavy naphtha. Both these streams are the…

Condensate Stabilization

Multistages Separation

Posted on September 16, 2009October 28, 2012

Figure 6-1 shows a multistage separation process. By removing molecules of the light components in the first separator they are not available to flash to…

Heat Exchangers

Separator Heat Exchangers

Posted on September 13, 2009

Heat exchangers used in gas production facilities are shell-and-tube, double-pipe, plate-and-frame, bath-type, forced-air, or direct-fired. In this chapter we will discuss the basic concepts for…

Heat Exchangers

Fired Heater Design

Posted on September 15, 2009October 29, 2012

Direct-fired combustion equipment is that in which the flame and/or products of combustion are used to achieve the desired result by radiation and convection. Common…

LTX Units and Line Heaters

LTX Wall Thickness Sizing

Posted on September 16, 2009October 28, 2012

Before choosing a wall thickness it is necessary to choose a pressure rating for the coil. Typically, the high-pressure coil (L1) is rated for the…

Water Treating Theory

Water Treating Coalescence

Posted on September 3, 2009

The process of coalescence in water treating systems is more time dependent than the process of dispersion. In dispersions of two immiscible liquids, immediate coalescence…

Pressure Drop in Piping

Moody Friction Factor

Posted on September 25, 2009October 28, 2012

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

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