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Type Of Devices

Rupture Discs

Posted on September 25, 2009

These are thin diaphragms held between flanges and calibrated to burst at a specified static inlet pressure. Unlike relief valves, rapture discs cannot reseal when…

Gas Processing

Gas Stripping Service

Posted on May 27, 2013

For stripping service, as in a glycol or amine contactor , bubble cap trays are the most common. In recent years, there has been a…

Fractions from atmospheric and vacuum distillation

Atmospheric Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the atmospheric distillation of the crude oil. Most crude oils are distilled in the atmospheric crude oil tower to…

Two Phase Oil and Gas Separation

Vertical Two Phase Separator Basic Design

Posted on August 17, 2009October 29, 2012

Figure 4-2 is a schematic of a vertical separator. In this configuration the inlet flow enters the vessel through the side. As in the horizontal…

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.…

Gas Processing

Physical Solvent Processes

Posted on August 20, 2020October 6, 2020

These processes are based on the solubility of the H2S and/or CO2 within the solvent, instead of on chemical reactions between the acid gas and…

Two Phase Separator Theory

Two Phase Separator Retention Time

Posted on September 14, 2009

To assure that the liquid and gas reach equilibrium at separator pressure a certain liquid storage is required. This is defined as “retention time” or…

Article

Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs

Posted on March 4, 2024March 4, 2024

Coriolis mass-flow controllers (MFCs) are widely used in the chemical process industries (CPI) for applications that require precise and accurate measurement and control of critical…

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…

Shell and Tube Exchangers

Shell and Tube Heat Exchanger Sizing

Posted on September 15, 2009October 29, 2012

The required heat duty, film coefficients, conductivity, etc. for a shell and tube heat exchanger can be calculated using the procedures in Heat Transfer Theory,…

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Recent Posts

  • Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs
  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
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  • 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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