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Heat Transfer Theory

Oil Sensible Heat Duty

Posted on September 13, 2009October 29, 2012

The sensible heat duty for the oil phase is: where Q0 = oil flow rate, bpd SG = oil specific gravity C0 = oil specific…

Hydrates

Hydrate Formation Temperature or Pressure Determination

Posted on September 15, 2009October 28, 2012

Knowledge of the temperature and pressure of a gas stream at the wellhead is important for determining whether hydrate formation can be expected when the…

Gas Processing

Structured Packing

Posted on May 27, 2013May 27, 2013

A bed of structured packing consists of a bed support upon which elements of structured packing are placed. Beds of structured packing typically have lower…

Fluid Properties

Molecular Weight of Gas

Posted on September 16, 2009October 29, 2012

The molecular weight of the stream is calculated from the weighted average gas molecular weight given by: The molecular weight of the gas stream of…

Production Process Component

Separator Control Valve

Posted on August 20, 2009October 30, 2012

Control valves are used throughout the process to control pressure, level, temperature, or flow. It is beyond the scope of this text to discussthe differences…

Two Phase Oil and Gas Separation

Spherical Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

A typical spherical separator is shown in Figure 4-3. The same four sections can be found in this vessel. Spherical separators are a special case…

Crude Oil Treating System

Coalescing Media

Posted on September 1, 2009

It is possible to use a coalescing media to promote coalescence of the water droplets. These media provide large surface area upon which water droplets…

Basic Separation

Cyclone Separator Capacity

Posted on October 24, 2023

Cyclone separators are widely used in various industries for the separation of solid particles from gas or liquid streams. The capacity of a cyclone separator…

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…

Fractions from atmospheric and vacuum distillation

Vacuum Distillation of Atmospheric Residue

Posted on September 26, 2009October 28, 2012

In modern refinery practice the distillation of atmospheric residue is accomplished under high vacuum conditions in a specially designed tower whose internal equipment ensures a…

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Recent Posts

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Categories

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  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
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  • 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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