Oil and Gas Separator

Skip to content
Menu
  • Home
  • Privacy Policy
  • Terms
  • Contact Us
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…

Two Phase Separator Equipment

Separator Inlet Diverters

Posted on August 17, 2009October 28, 2012

There are many types of inlet diverters. Two main types are baffle plates (shown in Figure 4-6) and centrifugal diverters (shown in Figure 4-7). A…

Shell and Tube Exchangers

Heat Exchanger Tubes

Posted on September 13, 2009October 31, 2012

Heat-exchanger tubes should not be confused with steel pipe or other types of pipe that are extruded to steel pipe sizes. The outside diameter of…

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…

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…

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…

Crude Oil Treating System

Horizontal Treaters Separator

Posted on September 2, 2009October 30, 2012

For most multi-well situations horizontal treaters are normally required. Figure 6-10 shows a typical design of a horizontal treater. Flow enters the front section of…

Crude Oil Treating System

Temperature Effects on Separation Process

Posted on September 1, 2009October 29, 2012

Adding heat to the incoming oil/water stream is the traditional method of separating the phases. The addition of heat reduces the viscosity of the oil…

Gas Processing

Proprietary Carbonate Systems

Posted on September 28, 2020October 6, 2020

Several proprietary processes have been developed based on the hot carbonate system with an activator or catalyst. These activators increase the performance of the hot…

Fluid Properties

Specific Gravity and Density

Posted on September 16, 2009October 29, 2012

Specific gravity of a liquid is the ratio of the density of the liquid at 60°F to the density of pure water. API gravity is…

Posts navigation

Previous Page Page 1 … Page 3 Page 4 Page 5 … 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