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Mechanical Design of Pressure Vessels

Separator Pressure Vessels Shop Drawings

Posted on September 24, 2009October 29, 2012

Before the vessel fabrication can proceed, the fabricator will develop complete drawings and have these drawings approved by the representative of the engineering firm and/or…

Fluid Properties

Liquid Specific Gravity

Posted on September 16, 2009October 29, 2012

Remembering that the weight of each component is the number of moles of that component times its molecular weight (pounds = MW X moles), the…

Two Phase Separator Equipment

Vortex Breakers Types

Posted on September 2, 2009October 28, 2012

It is normally a good idea to include a simple vortex breaker as shown in Figure 4-9 to keep a vortex from developing when the…

Two Phase Oil and Gas Separation

SEPARATOR TYPES

Posted on December 13, 2021December 13, 2021

There are four major types or basic configurations of separators, generally available from manufacturers which are as follows: 1. Vertical 2. Horizontal Single Tube 3.…

Water Treating Equipment

Disposal Piles

Posted on September 5, 2009

Disposal piles are large diameter (24- to 48-inch) open-ended pipes attached to the platform and extending below the surface of the water. Their main uses…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

Pressure Drop in Piping

Moody Friction Factor

Posted on September 25, 2009October 28, 2012

The factor of proportionality in the previous equations is called the  Moody friction factor and is determined from the Moody resistance diagram shown in Figure…

Two Phase Oil and Gas Separation

Maintain Optimum Pressure on Separator

Posted on December 13, 2021

For an oil and gas separator to accomplish its primary functions, pressure must be maintained in the separator so that the liquid and gas can…

Fractions from atmospheric and vacuum distillation

Straight Run Kerosene

Posted on September 26, 2009

This fraction is usually the first side stream of a conventional atmospheric distillation unit. It may be cut to meet a burning oil specification or…

Basic Configuration

Oil Treating Process

Posted on August 21, 2009October 31, 2012

Most oil treating on offshore facilities is done in vertical or horizontal treaters, such as those described in “Crude Oil Treating System“. Figure 2-8 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
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  • 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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