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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…

Gas Processing

Rectisol Process

Posted on May 27, 2013

The German Lurgi Company and Linde A. G. developed the Rectisol® process to use methanol to sweeten natural gas. Due to the high vapor pressure…

Produced Water Treating System

Pressure Vessel Drain System

Posted on September 5, 2009

A drain system that is connected directly to pressure vessels is called a “pressure” or “closed” drain system. A drain system that collects liquids that…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

Oil and Water Separation

Horizontal Three Phase Separator Part 2

Posted on August 21, 2009October 29, 2012

Figure 5-3 shows an alternate configuration known as a “bucket and weir” design. This design eliminates the need for a liquid interface controller. Both the…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

Three Phase Separator Sizing

Three Phase Vertical Separators Sizing

Posted on September 14, 2009October 30, 2012

As with vertical two-phase separators, a minimum diameter must be  maintained to assure adequate gas capacity. In addition, vertical threephase  separators must maintain a minimum…

Gas Processing

Solid Bed Absorption Process

Posted on May 27, 2013

A fixed bed of solid particles can be used to remove acid gases either through chemical reactions or ionic bonding. Typically, in solid bed absorption…

Separation

Process Separator Operating Pressure

Posted on August 20, 2009October 31, 2012

The choice of separator operating pressures in a multistage system is large. For large facilities many options should be investigated before a final choice is…

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…

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