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Pressure Drop in Piping

Reynolds Number Piping

Posted on September 25, 2009October 28, 2012

The Reynolds number is a dimensionless parameter that relates the ratio of inertial forces to viscous forces. It can be expressed by the following general…

Gas Processing

Structured Packing

Posted on May 27, 2013May 27, 2013

A bed of structured packing consists of a bed support upon which elements of structured packing are placed. Beds of structured packing typically have lower…

Water Treating Equipment

Precipitators Coalescing Filters Process

Posted on September 5, 2009October 31, 2012

In the past, it was common to direct the water to be treated through a bed of excelsior or another similar medium, as shown in…

Crude Oil Treating System

Electrostatic Treaters Process

Posted on September 2, 2009October 30, 2012

Some treaters use an electrode section. Figure 6-11 illustrates a typical design of a horizontal electrostatic treater. The flow path in an electrostatic treater is…

Crude Oil Treating System

Forming Emulsions Process

Posted on August 23, 2009October 31, 2012

For an emulsion to exist there must be two mutually immiscible liquids, an emulsifying agent, and sufficient agitation to disperse the discontinuous phase into the…

Pressure Relief

Relief Header Design

Posted on September 25, 2009October 28, 2012

The relief header is a system of piping connecting the outlets of all the relief valves into a common pipe or header that goes to…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

Basic Configuration

Oil Treating Process

Posted on August 21, 2009October 31, 2012

Most oil treating on offshore facilities is done in vertical or horizontal treaters, such as those described in “Crude Oil Treating System“. Figure 2-8 is…

Basic Separation

Horizontal Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

Separators are designed in either horizontal, vertical, or spherical configurations. Figure 4-1 is a schematic of a horizontal separator. The initial gross separation of liquid…

Shell and Tube Exchangers

TEMA Glasses and Tube Materials

Posted on September 15, 2009October 29, 2012

TEMA standards provide for two classes of shell and tube exchanger qualities. Class C is the lessĀ  stringent and is typically used in onshore applications…

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