Oil and Gas Separator

Skip to content
Menu
  • Home
  • Privacy Policy
  • Terms
  • Contact Us
Fractions from atmospheric and vacuum distillation

Atmospheric Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the atmospheric distillation of the crude oil. Most crude oils are distilled in the atmospheric crude oil tower to…

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:…

Heat Exchangers

Plate and Frame Exchangers

Posted on September 15, 2009October 29, 2012

Plate-and-frame exchangers are an arrangement of gasketed, pressed metal plates aligned on carrying bars and secured between two covers by compression bolts. The pressed metal…

Heat Transfer Theory

Oil Sensible Heat Duty

Posted on September 13, 2009October 29, 2012

The sensible heat duty for the oil phase is: where Q0 = oil flow rate, bpd SG = oil specific gravity C0 = oil specific…

Type Of Devices

Balanced Bellows Relief Valves

Posted on September 25, 2009October 28, 2012

Balanced relief valves are spring-loaded valves that contain a bellows arrangement to keep back-pressure from affecting the set point. Figure 13-4 shows a cross section…

Gas Processing

Random Packing

Posted on May 27, 2013May 27, 2013

A bed of random packing typically consists of a bed support (typically a gas injection support plate) upon which pieces of packing material are randomly…

Crude Oil Treating System

Coalescing Media

Posted on September 1, 2009

It is possible to use a coalescing media to promote coalescence of the water droplets. These media provide large surface area upon which water droplets…

Relief Valve Sizing

Two-Phase Flow Standard Sizes

Posted on September 25, 2009October 28, 2012

Two-Phase Flow There are no precise formulas for calculating orifice area for twophase flow. The common convention is to calculate the area required for the…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Vortex Breaker and Manways

Posted on September 24, 2009October 28, 2012

Vortex Breaker As liquid flows out of the exit nozzle, it will swirl and create a vortex. Vortexing would carry the gas out with the…

LTX Units and Line Heaters

LTX Coil Temperatures Sizing

Posted on September 16, 2009

In order to choose the coil length and diameter, a temperature must first be chosen upstream of the choke; the higher Th the longer the…

Posts navigation

Previous Page Page 1 … Page 4 Page 5 Page 6 … 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