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Two Phase Separator Theory

Two Phase Separator Retention Time

Posted on September 14, 2009

To assure that the liquid and gas reach equilibrium at separator pressure a certain liquid storage is required. This is defined as “retention time” or…

LTX Units and Line Heaters

LTX Units Heat Duty

Posted on September 15, 2009October 28, 2012

To calculate the heat duty it must be remembered that the pressure drop through the choke is instantaneous. That is, no heat is absorbed or…

Water Treating Equipment

Skim Pile

Posted on September 5, 2009October 31, 2012

The skim pile is a type of disposal pile. As shown in Figure 7-18, flow through the multiple series of baffle plates creates zones of…

Fluid Properties

Fluid Properties Viscosity Part 2

Posted on September 16, 2009October 29, 2012

In the absence of any laboratory data, correlations exist that relate viscosity  and temperature, given the oil gravity. The following equation  relating viscosity, gravity, and…

Production Process Component

Separation Temperature Control

Posted on August 20, 2009

The way in which the process temperature is controlled varies. In a heater, a temperature controller measures the process temperature and signals a fuel valve…

Shell and Tube Exchangers

Heat Exchanger Types

Posted on September 14, 2009October 29, 2012

There are many different arrangements of the shells, tubes and baffles in heat exchangers. Figure 3-6 is a list of TEMA standard classifications for heat…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Inspection Procedures

Posted on September 23, 2009

All ASME Code vessels are inspected by an approved Code inspector. The manufacturer will supply Code papers signed by the inspector. The nameplate on the…

Treater Vessels Sizing

Treaters Separator Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine the  diameter (d), length or height of the coalescing section (Leff or h),…

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…

Condensate Stabilization

Partial Pressure

Posted on September 16, 2009October 29, 2012

The fraction of any one component that flashes to gas at any stage in a process is a function of the temperature, pressure, and composition…

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