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Category: Treater Vessels Sizing

Treater Vessels Sizing

Example Sizing a Vertical Treater

Posted on October 6, 2009

Given: Oil gravity = 40°API, 0.875 S.G. Oil flow rate = 2,000 bpd Inlet oil temperature = 90°F Water S.G. = 1.04 Inlet BS&W =…

Treater Vessels Sizing

Example Sizing a Horizontal Treater

Posted on October 6, 2009

Given: Oil gravity = 30°API, 0.875 S.G. Oil flow rate = 5,000 bpd Inlet oil temperature = 80°F Water S.G. = 1.04 Inlet BS&W =10%…

Treater Vessels Sizing

Treaters Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine the  diameter (d), length or height of the coalescing section (Leff or h),…

Treater Vessels Sizing

Treaters Water Droplet Size

Posted on September 15, 2009

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…

Treater Vessels Sizing

Treater Retention Time Equations

Posted on September 15, 2009

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…

Treater Vessels Sizing

Treater Settling Equations

Posted on September 15, 2009

The specific gravity difference between the dispersed water droplets and the oil should result in the water “sinking” to the bottom of the treatment vessel.…

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