Oil and Gas Separator

Skip to content
Menu
  • Home
  • Privacy Policy
  • Terms
  • Contact Us
Gas Processing

Tray Efficiency and Tower Height

Posted on May 27, 2013

In condensate stabilizers, trays generally have 70% equilibrium stage efficiency. That is, 1.4 actual trays are required to provide one theoretical stage. The spacing between…

Fractions from atmospheric and vacuum distillation

Naphthas

Posted on September 26, 2009October 28, 2012

There are usually two naphtha cuts produced from most crude. These are: Light naphtha (sometimes called light gasoline) Heavy naphtha. Both these streams are the…

Treater Vessels Sizing

Treater Separator Settling Equations

Posted on September 15, 2009October 30, 2012

The specific gravity difference between the dispersed water droplets and the oil should result in the water “sinking” to the bottom of the treatment vessel.…

Potential Operating Problem

Sand Problems

Posted on September 2, 2009

Sand can be very troublesome in separators by causing cutout of valve trim, plugging of separator internals, and accumulation in the bottom of the separator.…

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…

Separation

Processes of magnetic separation

Posted on December 27, 2021

When a magnetizable solid is subjected to a magnetic induction field, the local magnetic moments are oriented in the direction of the induction fields, and…

Fluid Properties

Fluid Properties Viscosity Part 1

Posted on September 16, 2009October 29, 2012

This property of a fluid indicates its resistance to flow. It is a dynamic property, in that it can be measured only when the fluid…

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…

Water Treating Equipment

Skim Pile

Posted on September 5, 2009October 31, 2012

The skim pile is a type of disposal pile. As shown in Figure 7-18, flow through the multiple series of baffle plates creates zones of…

Crude Oil Treating System

Water Droplet Size and Retention Time

Posted on September 1, 2009

The droplet diameter is the most important single parameter to control to aid in water settling since this term is squared in the settling equation.…

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 2025 – Oil and Gas Separator
Wisteria Theme by WPFriendship ⋅ Powered by WordPress