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Heat Exchangers

Aerial Coolers Basic Principle Part 2

Posted on September 15, 2009October 28, 2012

Process outlet temperature in an aerial cooler can be controlled by louvers, fan variable speed drives, blade pitch or recirculation of process fluid. As the…

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…

Shell and Tube Exchangers

Heat Exchanger Placement of Fluid

Posted on September 14, 2009

The question always comes up of which fluid to put in the tubes and which fluid to put in the shell. Consider placing a fluid…

Produced Water Treating System

Pressure Vessel Drain System

Posted on September 5, 2009

A drain system that is connected directly to pressure vessels is called a “pressure” or “closed” drain system. A drain system that collects liquids that…

Treater Vessels Sizing

Treaters Water Separator Droplet Size

Posted on September 15, 2009October 30, 2012

In order to develop a treater design procedure, the water droplet size to be used in the settling equation to achieve a given outlet water…

Hydrates

Gas Expansion Temperature Drop

Posted on September 15, 2009October 30, 2012

Choking, or expansion of gas from a high pressure to a lower pressure, is generally required for control of gas flow rates. Choking is achieved…

Two Phase Oil and Gas Separation

OIL AND GAS SEPARATION DESIGN AND SIZING

Posted on December 13, 2021

Hydrocarbon streams as produced at the wellhead are composed of a mixture of gas, liquid hydrocarbons, and sometimes free water. In most cases it is…

Two Phase Oil and Gas Separation

Double Barrel and Filter Separator

Posted on August 17, 2009October 30, 2012

Cyclone separators are designed to operate by centrifugal force. These designs are best suited for fairly clean gas streams. The swirling action of the gas…

Oil and Water Separation

Horizontal Three Phase Separator Part 2

Posted on August 21, 2009October 29, 2012

Figure 5-3 shows an alternate configuration known as a “bucket and weir” design. This design eliminates the need for a liquid interface controller. Both the…

Mechanical Design of Pressure Vessels

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

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