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Water Treating Equipment

Disposal Piles

Posted on September 5, 2009

Disposal piles are large diameter (24- to 48-inch) open-ended pipes attached to the platform and extending below the surface of the water. Their main uses…

Two Phase Separator Equipment

Vortex Breakers Types

Posted on September 2, 2009October 28, 2012

It is normally a good idea to include a simple vortex breaker as shown in Figure 4-9 to keep a vortex from developing when the…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

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…

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…

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…

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…

Flotation Units

Dissolved Gas Units Design

Posted on September 5, 2009October 31, 2012

Dissolved gas designs take a portion of the treated water effluent and saturate the water with natural gas in a contactor. The higher the pressure…

Condensate Stabilization

Partial Pressure

Posted on September 16, 2009October 29, 2012

The fraction of any one component that flashes to gas at any stage in a process is a function of the temperature, pressure, and composition…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

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