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Mechanical Design of Pressure Vessels

Separator Pressure Vessels Nozzles

Posted on September 24, 2009October 29, 2012

Nozzles should be sized according to pipe sizing criteria, such as those provided in API RP 14E. The outlet nozzle is generally the same size…

Crude Oil Treating System

Oil Treating Systems Coalescence

Posted on September 1, 2009October 30, 2012

The process of coalescence in oil treating systems is time dependent. In dispersions of two immiscible liquids, immediate coalescence seldom occurs when two droplets collide.…

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…

Oil and Water Separation

Horizontal Three Phase Separator Part 1

Posted on August 21, 2009October 31, 2012

Three phase separator are designed as either horizontal or vertical pressure vessel. Figure 5-2 is a schematic of a horizontal separator. The fluid enters the…

Pressure Relief

Process Relief Requirements

Posted on September 25, 2009

The ASME code requires every pressure vessel that can be blocked In to have a relief valve to alleviate pressure build up due to thermal…

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…

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…

Mechanical Design of Pressure Vessels

Pressure Vessels Ladder and Platform

Posted on September 24, 2009October 29, 2012

Vessel Supports Small vertical vessels may be supported by angle support legs, as shown in Figure 12-11. Larger vertical vessels are generally supported by a…

Fluid Properties

Liquid Specific Gravity

Posted on September 16, 2009October 29, 2012

Remembering that the weight of each component is the number of moles of that component times its molecular weight (pounds = MW X moles), the…

LTX Units and Line Heaters

Line Heaters

Posted on September 15, 2009October 30, 2012

As shown in Figure 5-2, the well stream enters the first coil at its flowing tubing temperature and pressure. Alternatively, it could be choked at…

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Categories

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