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Heat Transfer Theory

Oil Sensible Heat Duty

Posted on September 13, 2009October 29, 2012

The sensible heat duty for the oil phase is: where Q0 = oil flow rate, bpd SG = oil specific gravity C0 = oil specific…

Two Phase Separator Equipment

Wave Breakers

Posted on August 17, 2009

In long horizontal vessels it is necessary to install wave breakers, which are nothing more than vertical baffles spanning the gas-liquid interface and perpendicular to…

Shell and Tube Exchangers

Heat Exchanger Placement of Fluid

Posted on September 14, 2009

The question always comes up of which fluid to put in the tubes and which fluid to put in the shell. Consider placing a fluid…

Heat Exchangers

Aerial Coolers Basic Principle Part 2

Posted on September 15, 2009October 28, 2012

Process outlet temperature in an aerial cooler can be controlled by louvers, fan variable speed drives, blade pitch or recirculation of process fluid. As the…

Type Of Devices

Conventional Relief Valves

Posted on September 25, 2009October 28, 2012

Figure 13-2 shows a cross section of a conventional relief valve and Figure 13-3 is a schematic that shows the valve’s operation. Convention al relief…

Crude Oil Treating System

Emulsifying Agent

Posted on August 30, 2009

When thinking about emulsion stability, it may be helpful to realize that in a pure oil and pure water mixture, without an emulsifying agent, no…

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…

Water Treating Equipment

Cross-Flow Separator

Posted on September 4, 2009October 31, 2012

Equipment manufacturers have modified the CPI configuration for horizontal water flow perpendicular to the axis of the corrugations in the plates as shown in Figure…

Two Phase Oil and Gas Separation

Vertical Two Phase Separator Basic Design

Posted on August 17, 2009October 29, 2012

Figure 4-2 is a schematic of a vertical separator. In this configuration the inlet flow enters the vessel through the side. As in the horizontal…

Pressure Relief

Relief Valve Installation

Posted on September 25, 2009

Each relief valve should be equipped with inlet piping no smaller than the valve inlet flange size, and inlet piping should be as short as…

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Recent Posts

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Categories

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  • Equations
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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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  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
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  • Type Of Devices
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  • Water Treating Theory
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