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LTX Units and Line Heaters

LTX Units Heat Duty

Posted on September 15, 2009October 28, 2012

To calculate the heat duty it must be remembered that the pressure drop through the choke is instantaneous. That is, no heat is absorbed or…

Shell and Tube Exchangers

Heat Exchanger Selections

Posted on September 14, 2009October 31, 2012

In selecting an exchanger, one must know the advantages and disadvantages of each type. The three basic types of shell-and-tube exchangers are fixed tube sheet,…

Gas Processing

Fluor Solvent Process

Posted on July 27, 2020October 6, 2020

This process uses propylene carbonate as a physical solvent to remove CO2 and H2S. Propylene carbonate also removes C2+ hydrocarbons, COS, SO2, CS2, and H2O…

Pressure Relief

Relief Valve Installation

Posted on September 25, 2009

Each relief valve should be equipped with inlet piping no smaller than the valve inlet flange size, and inlet piping should be as short as…

Condensate Stabilization

Partial Pressure

Posted on September 16, 2009October 29, 2012

The fraction of any one component that flashes to gas at any stage in a process is a function of the temperature, pressure, and composition…

Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

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…

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…

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…

Shell and Tube Exchangers

TEMA Glasses and Tube Materials

Posted on September 15, 2009October 29, 2012

TEMA standards provide for two classes of shell and tube exchanger qualities. Class C is the less  stringent and is typically used in onshore applications…

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