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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…

Two Phase Separator Theory

Two Phase Separator Settling Time

Posted on September 14, 2009October 30, 2012

In the gravity settling section the liquid drops will settle at a velocity determined by equating the gravity force on the drop with the drag…

Crude Oil Treating System

Temperature Effects on Separation Process

Posted on September 1, 2009October 29, 2012

Adding heat to the incoming oil/water stream is the traditional method of separating the phases. The addition of heat reduces the viscosity of the oil…

Gas Processing

Gas Stripping Service

Posted on May 27, 2013

For stripping service, as in a glycol or amine contactor , bubble cap trays are the most common. In recent years, there has been a…

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…

Water Treating Equipment

Cross-Flow Separator

Posted on September 4, 2009October 31, 2012

Equipment manufacturers have modified the CPI configuration for horizontal water flow perpendicular to the axis of the corrugations in the plates as shown in Figure…

LTX Units and Line Heaters

LTX Units

Posted on September 15, 2009October 28, 2012

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug…

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…

Water Treating Equipment

Parallel Plate Interceptor Design

Posted on September 4, 2009October 29, 2012

The first form of a plate coalescer was the parallel plate interceptor (PPI). This involved installing a series of plates parallel to the longitudinal axis…

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