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Hydrates

Water Vapor Condensation Process

Posted on September 15, 2009October 28, 2012

One method of assuring that hydrates do not form is to assure that the amount of water vapor in the gas is always less than…

Heat Exchangers

Double Pipe Heat Exchangers

Posted on September 15, 2009October 29, 2012

A double-pipe exchanger is made up of one pipe containing the tube fluid concentric with another pipe, which serves as the shell. The tube is…

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…

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…

Production Process Component

Separator Control Valve

Posted on August 20, 2009October 30, 2012

Control valves are used throughout the process to control pressure, level, temperature, or flow. It is beyond the scope of this text to discussthe differences…

Gas Processing

Distillation Service

Posted on May 27, 2013

For distillation services, as in condensate stabilization, tray design is well understood, and many engineers are more comfortable with trays than with packing. In the…

Potential Operating Problem

Foamy Crudes Problems

Posted on September 2, 2009

The major cause of foam in crude oil is the appearance of impurities, other than water, which are impractical to remove before the stream reaches…

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…

Crude Oil Treating System

Crude Oil Viscosity

Posted on September 1, 2009October 29, 2012

Laboratory testing of a particular oil at various temperatures is the most reliable method of determining how an oil behaves. ASTM D 341 outlines a…

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…

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