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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…

Hydrates

Water Vapor Condensation Process

Posted on September 15, 2009October 28, 2012

One method of assuring that hydrates do not form is to assure that the amount of water vapor in the gas is always less than…

Crude Oil Treating System

Crude Oil Treating System

Posted on August 23, 2009

Removing water from crude oil often requires additional processing beyond gravitational separation. In selecting a treating system, several factors should be considered to determine the…

Pressure Drop in Piping

Flow Regimes

Posted on September 25, 2009

Flow regimes describe the nature of fluid flow. There are two basic flow regimes for flow of a single-phase fluid: laminar flow and turbulent flow.…

Fractions from atmospheric and vacuum distillation

Vacuum Distillation of Atmospheric Residue

Posted on September 26, 2009October 28, 2012

In modern refinery practice the distillation of atmospheric residue is accomplished under high vacuum conditions in a specially designed tower whose internal equipment ensures a…

Water Treating Theory

Water Treating Dispersion

Posted on September 3, 2009October 28, 2012

An oscillating droplet of oil becomes unstable when the kinetic energy is sufficient to make up for the difference in the surface energy between the…

Basic Configuration

Water Treatment Process

Posted on August 21, 2009October 31, 2012

Water Treatment describes choosing a process for this subsystem, including vessel and open drains. Figure 2-13 shows an enlargement of the watertreating system for the…

Relief Valve Sizing

Effects of Back Pressure

Posted on September 25, 2009October 28, 2012

Back-pressure can affect either the set pressure or the capacity of a relief valve. The set pressure is the pressure at which the relief valve…

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…

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…

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