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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…

Gas Processing

Gas Sweetening Processes

Posted on May 27, 2013

Numerous processes have been developed for gas sweetening based on a variety of chemical and physical principles. These processes can be categorized by the principles…

Production Process Component

Separation Temperature Control

Posted on August 20, 2009

The way in which the process temperature is controlled varies. In a heater, a temperature controller measures the process temperature and signals a fuel valve…

Mechanical Design of Pressure Vessels

Pressure Vessels Maximum Allowable Stress Values

Posted on September 23, 2009October 29, 2012

The maximum allowable stress values to be used in the calculation of the vessel’s wall thickness are given in the ASME Code for many different…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

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…

Crude Oil Treating System

Horizontal Treaters Separator

Posted on September 2, 2009October 30, 2012

For most multi-well situations horizontal treaters are normally required. Figure 6-10 shows a typical design of a horizontal treater. Flow enters the front section of…

Pressure Relief

Relief Valve Vent or Flare Tip

Posted on September 25, 2009

A pipe that releases gas to disperse into the atmosphere is called a vent. If the gas is burned at the tip, it is called…

Water Treating Theory

Water Treating Coalescence

Posted on September 3, 2009

The process of coalescence in water treating systems is more time dependent than the process of dispersion. In dispersions of two immiscible liquids, immediate coalescence…

Pressure Drop in Piping

Bernoulli’s Theorem

Posted on September 25, 2009October 28, 2012

It is customary to express the energy contained in a fluid in terms of the potential energy contained in an equivalent height or “head” of…

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Categories

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