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Production Process Component

Separation Flow Control

Posted on August 20, 2009

It is very rare that flow must be controlled in an oil field process. Normally, the control of pressure, level, and temperature is sufficient. Occasionally,…

Water Treating Theory

Water Treating Flotation

Posted on September 3, 2009

The process of flotation improves the separation of the oil droplets from the water continuous phase. This goal is accomplished by increasing the difference in…

Basic Configuration

Lease Automatic Custudy Transfer

Posted on August 21, 2009October 29, 2012

In large facilities oil is typically sold through a LACT unit, which is designed to meet API Standards and whatever additional measuring and sampling standards…

Mechanical Design of Pressure Vessels

Pressure Vessels Maximum Allowable Stress Values

Posted on September 23, 2009October 29, 2012

The maximum allowable stress values to be used in the calculation of the vessel’s wall thickness are given in the ASME Code for many different…

Article

Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs

Posted on March 4, 2024March 4, 2024

Coriolis mass-flow controllers (MFCs) are widely used in the chemical process industries (CPI) for applications that require precise and accurate measurement and control of critical…

Two Phase Separator Theory

Two Phase Separator Drop Size

Posted on September 14, 2009

The purpose of the gas separation section of the vessel is to condition the gas for final polishing by the mist extractor. From field experience…

Flotation Units

Dispersed Gas Units Sizing

Posted on September 5, 2009

It can be shown mathematically that an efficient design must have a high gas induction rate, a small diameter induced gas bubble, and relatively large…

Separation

Stages Separation Selection

Posted on August 20, 2009October 29, 2012

As more stages are added to the process there is less and less incremental liquid recovery. The diminishing income for adding a stage must more…

Water Treating Equipment

Parallel Plate Interceptor Design

Posted on September 4, 2009October 29, 2012

The first form of a plate coalescer was the parallel plate interceptor (PPI). This involved installing a series of plates parallel to the longitudinal axis…

Pressure Drop in Piping

Moody Friction Factor

Posted on September 25, 2009October 28, 2012

The factor of proportionality in the previous equations is called theĀ  Moody friction factor and is determined from the Moody resistance diagram shown in Figure…

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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
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  • 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
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  • 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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