Oil & Gas Process Engineering

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

Tag: Condensate Stabilization

Trays and Packing

Trays

Posted on September 17, 2009

For most trays, liquid flows across an “active area” of the tray and then into a “downcomer” to the next tray below, etc. Inlet and/or…

Trays and Packing

Sieve Trays

Posted on September 17, 2009

Sieve trays are the least expensive tray option. In sieve trays, vapor flowing up through the tower contacts the liquid by passing through small perforations…

Trays and Packing

Trays and Packing

Posted on September 17, 2009

The number of actual equilibrium stages determines the number of flashes that will occur. The more stages, the more complete the split, but the taller…

Condensate Stabilization

Condensate Stabilizer Design

Posted on September 17, 2009

It can be seen from the previous description that the design of both a cold-feed stabilizer and a stabilizer with reflux is a rather complex…

Condensate Stabilization

Distillation Tower with Reflux

Posted on September 17, 2009

Figure 6-5 shows a stabilizer with reflux. The well fluid is heated with the bottoms product and injected into the tower, below the top, where…

Condensate Stabilization

Cold Feed Distillation Tower

Posted on September 17, 2009

Figure 6-4 shows the cold feed distillation tower of Figure 6-3. The inlet stream enters the top of the tower. It is heated by the…

Condensate Stabilization

Multiple Flashes at Constant Pressure and Increasing Temperature

Posted on September 17, 2009

It is possible to stabilize a liquid at a constant pressure by successively flashing it at increasing temperatures as shown in Figure 6-2. At each…

Condensate Stabilization

Multistages Separation

Posted on September 16, 2009

Figure 6-1 shows a multistage separation process. By removing molecules of the light components in the first separator they are not available to flash to…

Condensate Stabilization

Partial Pressure

Posted on September 16, 2009

The fraction of any one component that flashes to gas at any stage in a process is a function of the temperature, pressure, and composition…

Posts navigation

Previous Page Page 1 Page 2

Pages

  • Contact Us
  • Privacy Policy
  • Terms

Categories

  • Acid Gas Treating
  • Article
  • Basic Configuration
  • Basic Principles
  • Centrifugal Compressors
  • Centrifugal Pumps
  • Centrifugal Pumps Bearings-Seals-Wear-Rings
  • Characterizing the Flow Stream
  • Chemical Process
  • Chemical Solvents
  • Choise Of Process
  • Coil Sizing
  • Compressors
  • Condensate Stabilization
  • Controlling Pulsating Flow
  • Cooling and Lubricating System
  • Crude Oil Treating System
  • Cylinder Sizing
  • Design Considerations
  • Design Considerations
  • Design Procedures for Amine System
  • Direct Conversion of H2S to Sulfur
  • Emulsion Treating Teory
  • Equations
  • Flotation Units
  • Fluid Properties – Basic Principles
  • Fractions from atmospheric and vacuum distillation
  • Gas
  • Gas Dehydration
  • Gas Processing
  • Gas Sweetening Processes
  • Gas Turbine
  • Generic Types of Centrifugal Pumps
  • Glycol Dehydration
  • Glycol Dehydration
  • Gravity Separation
  • Heat Exchangers
  • Hydrates
  • Hydrocarbon
  • Ideas To Enhance Gas Flow
  • Influent Water Quality
  • Installation
  • Instrumentation
  • Liquid Loading
  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • Mechanisms of Heat Transfer
  • News
  • Oil and Gas Processing
  • Oil and Water Separation
  • Oil Production Facility
  • Petrochemical
  • Physical Solvent Processes
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
  • Pressure Relieving Systems GP
  • Pressure Vessels – Design
  • Process Cooling in Remote Location
  • Process Heat Duty
  • Produced Water Treating System
  • Production Process Component
  • Pumps
  • Reboiler
  • Reciprocating Compressors
  • RECIPROCATING COMPRESSORS
  • Reciprocating Compressors – Components
  • Refining
  • Relief Valve Sizing
  • Separation
  • Separation
  • Shell and Tube Exchangers
  • Solid Bed Absorption
  • Solid Bed Dehydration
  • Specification and Design
  • Three Phase Separator Sizing
  • Tower Pressure
  • Tray
  • Trays and Packing
  • Treater Vessels Sizing
  • Treating Equipment
  • Two Phase Oil and Gas Separation
  • Two Phase Separator Equipment
  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
  • Types Of Compressors
  • Uncategorized
  • Water Treating Equipment
  • Water Treating Theory
  • Well Site Troubleshooting
  • Wellhead Compression
  • Wellhead Surface Equipment

Recent Posts

  • ABS – Mass process by Technip Stone & Webster Process Technology
  • ABS Emulsion process by Technip Stone & Webster Process Technology
  • Revolutionizing Renewables: CO2 to Methanol at Standard Conditions
  • 1,3 Butadiene Process by BASF SE/Air Liquide Global E&C Solutions Germany GmbH
  • New Fortress Energy launches Barcarena LNG terminal in Brazil
© Copyright 2025 – Oil & Gas Process Engineering
Wisteria Theme by WPFriendship ⋅ Powered by WordPress