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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…

Treater Vessels Sizing

Treaters Separator Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine theĀ  diameter (d), length or height of the coalescing section (Leff or h),…

Equations

Head Bernoulli Equation in Process Engineering

Posted on February 9, 2024

Head Bernoulli is a term that refers to the total energy of a fluid at a given point in a steady flow system. It consists…

Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

Three Phase Separator Sizing

Three Phase Horizontal Separator Sizing

Posted on September 14, 2009October 30, 2012

For sizing a horizontal three-phase separator it is necessary to specify a vessel diameter and a seam-to-seam vessel length. The gas capacity and retention time…

Relief Valve Sizing

Effects of Back Pressure

Posted on September 25, 2009October 28, 2012

Back-pressure can affect either the set pressure or the capacity of a relief valve. The set pressure is the pressure at which the relief valve…

Mechanical Design of Pressure Vessels

Pressure Vessels Relief Devices and Corrosion Protection

Posted on September 24, 2009

Pressure Relief Devices All pressure vessels should be equipped with one or more pressure safety valves (PSVs) to prevent overpressure. This is a requirement of…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Specifications

Posted on September 24, 2009October 29, 2012

Most companies have a detailed general specification for the construction of pressure vessels, which defines the overall quality of fabrication required and addresses specific items…

Heat Exchangers

Aerial Coolers Part 1

Posted on September 15, 2009October 28, 2012

Aerial coolers are often used to cool a hot fluid to near ambient temperature. They are mechanically simple and flexible, and they eliminate the nuisance…

Separation

Process Separator Operating Pressure

Posted on August 20, 2009October 31, 2012

The choice of separator operating pressures in a multistage system is large. For large facilities many options should be investigated before a final choice is…

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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

  • Article
  • Basic Configuration
  • Basic Separation
  • Condensate Stabilization
  • Crude Oil Treating System
  • Equations
  • Flotation Units
  • Fluid Properties
  • Fractions from atmospheric and vacuum distillation
  • Gas Processing
  • Heat Exchangers
  • Heat Transfer Theory
  • Hydrates
  • 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
  • Separation
  • 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
  • Water Treating Equipment
  • Water Treating Theory
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