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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…

Basic Configuration

Water Treatment Process

Posted on August 21, 2009October 31, 2012

Water Treatment describes choosing a process for this subsystem, including vessel and open drains. Figure 2-13 shows an enlargement of the watertreating system for the…

Crude Oil Treating System

Gravity Separation Process

Posted on August 31, 2009October 30, 2012

Most oil-treating equipment relies on gravity to separate water droplets from the oil continuous phase, because water droplets are heavier than the volume of oil…

Pressure Drop in Piping

Flow Regimes

Posted on September 25, 2009

Flow regimes describe the nature of fluid flow. There are two basic flow regimes for flow of a single-phase fluid: laminar flow and turbulent flow.…

Treater Vessels Sizing

Treaters Water Separator Droplet Size

Posted on September 15, 2009October 30, 2012

In order to develop a treater design procedure, the water droplet size to be used in the settling equation to achieve a given outlet water…

Separation

Process Separator Operating Pressure

Posted on August 20, 2009October 31, 2012

The choice of separator operating pressures in a multistage system is large. For large facilities many options should be investigated before a final choice is…

Two Phase Oil and Gas Separation

Maintain Optimum Pressure on Separator

Posted on December 13, 2021

For an oil and gas separator to accomplish its primary functions, pressure must be maintained in the separator so that the liquid and gas can…

Water Treating Equipment

Precipitators Coalescing Filters Process

Posted on September 5, 2009October 31, 2012

In the past, it was common to direct the water to be treated through a bed of excelsior or another similar medium, as shown in…

Water Treating Equipment

Corrugated Plate Interceptor Design

Posted on September 4, 2009October 31, 2012

The most common form of parallel plate interceptor used in oil facilities is the corrugated plate interceptor (CPI). This is a refinement of the PPI…

Mechanical Design of Pressure Vessels

Estimating Pressure Vessels Weights

Posted on September 23, 2009October 29, 2012

It is important to be able to estimate vessel weights, since most cost estimating procedures start with the weight of the vessel. The vessel weight,…

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Categories

  • Article
  • Basic Configuration
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  • Equations
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  • 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
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  • Water Treating Theory
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