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LTX Units and Line Heaters

LTX Coil Diameter Sizing

Posted on September 16, 2009October 28, 2012

Erosional flow criteria will almost always govern in choosing the diameter. Sometimes it is necessary to check for pressure drop in the coil. Typically, pressure…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

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…

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:…

Water Treating Equipment

Precipitators Coalescing Filters Process

Posted on September 5, 2009October 31, 2012

In the past, it was common to direct the water to be treated through a bed of excelsior or another similar medium, as shown in…

Heat Exchangers

Fired Heater Design

Posted on September 15, 2009October 29, 2012

Direct-fired combustion equipment is that in which the flame and/or products of combustion are used to achieve the desired result by radiation and convection. Common…

Relief Valve Sizing

Liquids Flow Rate

Posted on September 25, 2009October 28, 2012

Conventional Valve, Balanced-Bellows Valve, or Pilot-Operated Valve The corresponding equations for liquid flow are the following: Note that a preliminary orifice size must be determined…

Shell and Tube Exchangers

Heat Exchanger Tube Pitch

Posted on September 13, 2009October 31, 2012

Tube holes cannot be drilled very close together, since this may structually weaken the tube sheet. The shortest distance between two adjacent tube holes is…

Treater Vessels Sizing

Treater Separator Retention Time Equations

Posted on September 15, 2009October 30, 2012

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…

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