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Treater Vessels Sizing

Treater Separator Retention Time Equations

Posted on September 15, 2009October 30, 2012

The oil must be held at temperature for a specific period of time to enable de-emulsifying the water-in-oil emulsion. This information is best determined in…

LTX Units and Line Heaters

LTX Coil Temperatures Sizing

Posted on September 16, 2009

In order to choose the coil length and diameter, a temperature must first be chosen upstream of the choke; the higher Th the longer the…

Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

Two Phase Separator Sizing

Two Phase Horizontal Separators Sizing

Posted on September 14, 2009October 30, 2012

For sizing a horizontal separator it is necessary to choose a seam-toseam  vessel length and a diameter. This choice must satisfy the conditions  for gas…

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…

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…

Two Phase Separator Equipment

Wave Breakers

Posted on August 17, 2009

In long horizontal vessels it is necessary to install wave breakers, which are nothing more than vertical baffles spanning the gas-liquid interface and perpendicular to…

Mechanical Design of Pressure Vessels

Pressure Vessels Relief Devices and Corrosion Protection

Posted on September 24, 2009

Pressure Relief Devices All pressure vessels should be equipped with one or more pressure safety valves (PSVs) to prevent overpressure. This is a requirement of…

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…

Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

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Categories

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