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Fluid Properties

Gas Flow Rate

Posted on September 16, 2009October 29, 2012

If the flow rate of the inlet stream is known in moles per day then the number of moles per day of gas flow can…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Nozzles

Posted on September 24, 2009October 29, 2012

Nozzles should be sized according to pipe sizing criteria, such as those provided in API RP 14E. The outlet nozzle is generally the same size…

Produced Water Treating System

Pressure Vessel Drain System

Posted on September 5, 2009

A drain system that is connected directly to pressure vessels is called a “pressure” or “closed” drain system. A drain system that collects liquids that…

Production Process Component

Separation Flow Control

Posted on August 20, 2009

It is very rare that flow must be controlled in an oil field process. Normally, the control of pressure, level, and temperature is sufficient. Occasionally,…

Fractions from atmospheric and vacuum distillation

Naphthas

Posted on September 26, 2009October 28, 2012

There are usually two naphtha cuts produced from most crude. These are: Light naphtha (sometimes called light gasoline) Heavy naphtha. Both these streams are the…

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…

Two Phase Oil and Gas Separation

OIL AND GAS SEPARATION DESIGN AND SIZING

Posted on December 13, 2021

Hydrocarbon streams as produced at the wellhead are composed of a mixture of gas, liquid hydrocarbons, and sometimes free water. In most cases it is…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Temperature Design

Posted on September 23, 2009

The maximum and minimum design temperatures for a vessel will determine the maximum allowable stress value permitted for the material to be used in the…

Heat Exchangers

Aerial Coolers Basic Principle Part 2

Posted on September 15, 2009October 28, 2012

Process outlet temperature in an aerial cooler can be controlled by louvers, fan variable speed drives, blade pitch or recirculation of process fluid. As the…

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.…

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Categories

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  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
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  • Type Of Devices
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