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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…

Shell and Tube Exchangers

Heat Exchanger Types

Posted on September 14, 2009October 29, 2012

There are many different arrangements of the shells, tubes and baffles in heat exchangers. Figure 3-6 is a list of TEMA standard classifications for heat…

Shell and Tube Exchangers

Heat Exchanger Placement of Fluid

Posted on September 14, 2009

The question always comes up of which fluid to put in the tubes and which fluid to put in the shell. Consider placing a fluid…

Two Phase Separator Sizing

Two Phase Vertical Separators Sizing

Posted on September 14, 2009October 30, 2012

In vertical separators, a minimum diameter must be maintained to allow liquid drops to separate from the vertically moving gas. The liquid retention time requirement…

Hydrates

Kinetic Inhibitor Process

Posted on September 15, 2009

A kinetic inhibitor is a polymeric chemical that, when added to a production stream, will not change the hydrate formation temperature but will delay the…

Pressure Relief

Process Relief Requirements

Posted on September 25, 2009

The ASME code requires every pressure vessel that can be blocked In to have a relief valve to alleviate pressure build up due to thermal…

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…

LTX Units and Line Heaters

LTX Coil Lengths Sizing

Posted on September 16, 2009October 28, 2012

With the known temperatures on each end of the coil, the heat duty for each coil can be calculated from the heat transfer theory. Since…

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.…

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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Recent Posts

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Categories

  • Article
  • Basic Configuration
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  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
  • Heat Exchangers
  • Heat Transfer Theory
  • Hydrates
  • Influent Water Quality
  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
  • Produced Water Treating System
  • Production Process Component
  • Relief Valve Sizing
  • Separation
  • Separation
  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
  • Two Phase Separator Equipment
  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
  • Water Treating Equipment
  • Water Treating Theory
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