Oil and Gas Separator

Skip to content
Menu
  • Home
  • Privacy Policy
  • Terms
  • Contact Us
Pressure Drop in Piping

Moody Friction Factor

Posted on September 25, 2009October 28, 2012

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

Gas Processing

Gas Processing Plant Condensate Stabilizer

Posted on May 27, 2013

A gas-processing plant, is designed to recover ethane, propane, butane, and other natural gas liquids from the gas stream. A condensate stabilizer also recovers some…

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…

Separation

Intensity of magnetization and magnetic separation

Posted on December 27, 2021

When subjected to a magnetic induction B, an elementary volume v of magnetizable substance acquires local magnetization M, where M is the magnetic moment of…

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…

Pressure Relief

Pressure Relief Valves

Posted on September 25, 2009

The most important safety devices in a production facility are the pressure relief valves, which ensure that pipes, valves, fittings, and pressure vessels can never…

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…

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…

Shell and Tube Exchangers

TEMA Glasses and Tube Materials

Posted on September 15, 2009October 29, 2012

TEMA standards provide for two classes of shell and tube exchanger qualities. Class C is the lessĀ  stringent and is typically used in onshore applications…

LTX Units and Line Heaters

Fire Tube Sizing

Posted on September 16, 2009October 28, 2012

The area of the fire tube is normally calculated based on a heat flux rate of 10,000 Btu/hr-ft2. The fire-tube length can be determined from:…

Posts navigation

Previous Page Page 1 Page 2 Page 3 … Page 20 Next Page

Pages

  • Contact Us
  • Privacy Policy
  • Terms

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
© Copyright 2026 – Oil and Gas Separator
Wisteria Theme by WPFriendship ⋅ Powered by WordPress