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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.…

Fluid Properties

The Flow Stream

Posted on September 16, 2009October 29, 2012

Many times the designer is given the mole fraction of each component in the feed stream but is not given the mole flow rate for…

LTX Units and Line Heaters

LTX Unit Condensate Stabilizer

Posted on May 27, 2013

It should be clear from the description of LTX units that the lower pressure separator in an LTX unit is a simple form of cold-feed…

Water Treating Equipment

SP Pack Separator

Posted on September 5, 2009October 31, 2012

The gravity settling devices previously discussed make use of closely spaced internals to reduce the distance an oil droplet must rise to meet a coalescing…

Fluid Properties

Liquid Specific Gravity

Posted on September 16, 2009October 29, 2012

Remembering that the weight of each component is the number of moles of that component times its molecular weight (pounds = MW X moles), the…

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…

Shell and Tube Exchangers

Shell and Tube Heat Exchanger Sizing

Posted on September 15, 2009October 29, 2012

The required heat duty, film coefficients, conductivity, etc. for a shell and tube heat exchanger can be calculated using the procedures in Heat Transfer Theory,…

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…

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…

Potential Operating Problem

Liquid Carryover and Gas Blowby

Posted on September 2, 2009

Liquid carryover and gas blowby are two common operating problems. Liquid carryover occurs when free liquid escapes with the gas phase and can indicate high…

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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
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