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Mechanical Design of Pressure Vessels

Pressure Vessels Maximum Allowable Stress Values

Posted on September 23, 2009October 29, 2012

The maximum allowable stress values to be used in the calculation of the vessel’s wall thickness are given in the ASME Code for many different…

Gas Processing

Tray Efficiency and Tower Height

Posted on May 27, 2013

In condensate stabilizers, trays generally have 70% equilibrium stage efficiency. That is, 1.4 actual trays are required to provide one theoretical stage. The spacing between…

LTX Units and Line Heaters

Fire Tube Sizing

Posted on September 16, 2009October 28, 2012

The area of the fire tube is normally calculated based on a heat flux rate of 10,000 Btu/hr-ft2. The fire-tube length can be determined from:…

Two Phase Oil and Gas Separation

Vertical Two Phase Separator Basic Design

Posted on August 17, 2009October 29, 2012

Figure 4-2 is a schematic of a vertical separator. In this configuration the inlet flow enters the vessel through the side. As in the horizontal…

Fluid Properties

Molecular Weight of Gas

Posted on September 16, 2009October 29, 2012

The molecular weight of the stream is calculated from the weighted average gas molecular weight given by: The molecular weight of the gas stream of…

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 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…

Relief Valve Sizing

Critical Flow

Posted on September 25, 2009October 28, 2012

The flow of a compressible fluid through an orifice is limited by critical flow. Critical flow is also referred to as choked flow, sonic flow,…

Potential Operating Problem

Foamy Crudes Problems

Posted on September 2, 2009

The major cause of foam in crude oil is the appearance of impurities, other than water, which are impractical to remove before the stream reaches…

Crude Oil Treating System

Gravity Separation Process

Posted on August 31, 2009October 30, 2012

Most oil-treating equipment relies on gravity to separate water droplets from the oil continuous phase, because water droplets are heavier than the volume of oil…

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