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Oil and Water Separation

Vessel Internal Design

Posted on September 2, 2009

Two common internals not discussed are coalescing plates and sand jets. It is possible to use various plate or pipe coalescer designs to aid in…

Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

Two Phase Oil and Gas Separation

OIL AND GAS SEPARATION DESIGN AND SIZING

Posted on December 13, 2021

Hydrocarbon streams as produced at the wellhead are composed of a mixture of gas, liquid hydrocarbons, and sometimes free water. In most cases it is…

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…

Two Phase Oil and Gas Separation

INTERNAL CONSTRUCTION OF SEPARATORS

Posted on December 13, 2021December 13, 2021

The principal items of construction that should be present in a good liquid-gas separator are the same regardless of the over-al1 shape or configuration of…

Two Phase Separator Equipment

Separator Inlet Diverters

Posted on August 17, 2009October 28, 2012

There are many types of inlet diverters. Two main types are baffle plates (shown in Figure 4-6) and centrifugal diverters (shown in Figure 4-7). A…

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…

Mechanical Design of Pressure Vessels

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

Fluid Properties

Gas Flow Rate

Posted on September 16, 2009October 29, 2012

If the flow rate of the inlet stream is known in moles per day then the number of moles per day of gas flow can…

Two Phase Oil and Gas Separation

Spherical Two Phase Separator Basic Design

Posted on August 17, 2009October 30, 2012

A typical spherical separator is shown in Figure 4-3. The same four sections can be found in this vessel. Spherical separators are a special case…

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Categories

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  • Fractions from atmospheric and vacuum distillation
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  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
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  • Water Treating Theory
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