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Fluid Properties

Liquid Molecular Weight Calculation

Posted on September 16, 2009October 29, 2012

The molecular weight of the liquid stream is calculated from the weighted average liquid component molecular weight given by: This is calculated in Table 3-3.…

Influent Water Quality

Water Treating System Produced Water

Posted on September 5, 2009October 31, 2012

The first step in choosing a water treating system is to characterize the influent water streams. It is necessary to know both the oil concentration…

LTX Units and Line Heaters

LTX Units

Posted on September 15, 2009October 28, 2012

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug…

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…

Basic Configuration

Water Treatment Process

Posted on August 21, 2009October 31, 2012

Water Treatment describes choosing a process for this subsystem, including vessel and open drains. Figure 2-13 shows an enlargement of the watertreating system for the…

Gas Processing

Sulfinol Process

Posted on September 10, 2020October 6, 2020

Licensed by Shell the SulfinolĀ® process combines the properties of a physical and a chemical solvent. The Sulfinol solution consists of a mixture of sulfolane…

Shell and Tube Exchangers

Heat Exchanger Baffles

Posted on September 13, 2009October 31, 2012

Shell-and-tube exchangers contain several types of baffles to help direct the flow of both tube-side and shell-side fluids. Pass partition baffles force the fluid to…

LTX Units and Line Heaters

Line Heaters

Posted on September 15, 2009October 30, 2012

As shown in Figure 5-2, the well stream enters the first coil at its flowing tubing temperature and pressure. Alternatively, it could be choked at…

Pressure Drop in Piping

Flow Regimes

Posted on September 25, 2009

Flow regimes describe the nature of fluid flow. There are two basic flow regimes for flow of a single-phase fluid: laminar flow and turbulent flow.…

Fractions from atmospheric and vacuum distillation

Straight Run Kerosene

Posted on September 26, 2009

This fraction is usually the first side stream of a conventional atmospheric distillation unit. It may be cut to meet a burning oil specification or…

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Recent Posts

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Categories

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  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
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  • Heat Transfer Theory
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  • 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
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  • 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
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  • Water Treating Theory
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