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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…

Oil and Water Separation

Vertical Three Phase Separator Configuration

Posted on September 2, 2009October 29, 2012

Figure 5-6 shows a typical configuration for a vertical three-phase separator. Flow enters the vessel through the side as in the horizontal separator, the inlet…

Basic Separation

Horizontal Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

Separators are designed in either horizontal, vertical, or spherical configurations. Figure 4-1 is a schematic of a horizontal separator. The initial gross separation of liquid…

Crude Oil Treating System

Emulsifying Agent

Posted on August 30, 2009

When thinking about emulsion stability, it may be helpful to realize that in a pure oil and pure water mixture, without an emulsifying agent, no…

Potential Operating Problem

Sand Problems

Posted on September 2, 2009

Sand can be very troublesome in separators by causing cutout of valve trim, plugging of separator internals, and accumulation in the bottom of the separator.…

Two Phase Oil and Gas Separation

INTERNAL CONSTRUCTION OF SEPARATORS

Posted on December 13, 2021December 13, 2021

The principal items of construction that should be present in a good liquid-gas separator are the same regardless of the over-al1 shape or configuration of…

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…

Gas Processing

Iron Sponge Process

Posted on May 27, 2013May 27, 2013

The iron sponge process uses the chemical reaction of ferric oxide with H2S to sweeten gas streams. This process is applied to gases with low…

Heat Exchangers

Separator Heat Exchangers

Posted on September 13, 2009

Heat exchangers used in gas production facilities are shell-and-tube, double-pipe, plate-and-frame, bath-type, forced-air, or direct-fired. In this chapter we will discuss the basic concepts for…

Water Treating Theory

Water Treating Coalescence

Posted on September 3, 2009

The process of coalescence in water treating systems is more time dependent than the process of dispersion. In dispersions of two immiscible liquids, immediate coalescence…

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Recent Posts

  • Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs
  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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