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Author: peter

Two Phase Separator Theory

Two Phase Separator Drop Size

Posted on September 14, 2009September 15, 2014 by peter

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…

Two Phase Separator Theory

Two Phase Separator Settling Time

Posted on September 14, 2009September 15, 2014 by peter

In the gravity settling section the liquid drops will settle at a velocity determined by equating the gravity force on the drop with the drag…

Shell and Tube Exchangers

Heat Exchanger Tube Pitch

Posted on September 13, 2009September 16, 2014 by peter

Tube holes cannot be drilled very close together, since this may structually weaken the tube sheet. The shortest distance between two adjacent tube holes is…

Shell and Tube Exchangers

Heat Exchanger Tubes

Posted on September 13, 2009September 16, 2014 by peter

Heat-exchanger tubes should not be confused with steel pipe or other types of pipe that are extruded to steel pipe sizes. The outside diameter of…

Shell and Tube Exchangers

Heat Exchanger Baffles

Posted on September 13, 2009September 11, 2014 by peter

Shell-and-tube exchangers contain several types of baffles to help direct the flow of both tube-side and shell-side fluids. Pass partition baffles force the fluid to…

Shell and Tube Exchangers

Shell and Tube Exchangers

Posted on September 13, 2009September 16, 2014 by peter

Shell-and-tube heat exchangers are cylindrical in shape, consisting of a bundle of parallel tubes surrounded by an outer casing (shell). Both the tube bundle and…

Oil and Gas Separator

Oil Sensible Heat Duty

Posted on September 13, 2009September 15, 2014 by peter

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

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