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Pressure Relief

Process Relief Requirements

Posted on September 25, 2009

The ASME code requires every pressure vessel that can be blocked In to have a relief valve to alleviate pressure build up due to thermal…

Two Phase Oil and Gas Separation

Double Barrel and Filter Separator

Posted on August 17, 2009October 30, 2012

Cyclone separators are designed to operate by centrifugal force. These designs are best suited for fairly clean gas streams. The swirling action of the gas…

Hydrates

Kinetic Inhibitor Process

Posted on September 15, 2009

A kinetic inhibitor is a polymeric chemical that, when added to a production stream, will not change the hydrate formation temperature but will delay the…

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…

Hydrates

Gas Expansion Temperature Drop

Posted on September 15, 2009October 30, 2012

Choking, or expansion of gas from a high pressure to a lower pressure, is generally required for control of gas flow rates. Choking is achieved…

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…

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.…

LTX Units and Line Heaters

LTX Units

Posted on September 15, 2009October 28, 2012

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug…

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…

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.…

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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
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  • Cyclone Separator Capacity

Categories

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  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
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  • 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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