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Shell and Tube Exchangers

Heat Exchanger Tube Pitch

Posted on September 13, 2009October 31, 2012

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…

Fluid Properties

The Flow Stream

Posted on September 16, 2009October 29, 2012

Many times the designer is given the mole fraction of each component in the feed stream but is not given the mole flow rate for…

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…

Mechanical Design of Pressure Vessels

Determining Separator Pressure Vessels Wall Thickness

Posted on September 23, 2009October 29, 2012

The following formulas are used in the ASME Code Section VIII, Division 1 for determining wall thickness: Wall thickness—cylindrical shells Figure 12-1 defines the various…

Fluid Properties

Liquid Molecular Weight Calculation

Posted on September 16, 2009October 29, 2012

The molecular weight of the liquid stream is calculated from the weighted average liquid component molecular weight given by: This is calculated in Table 3-3.…

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…

Equations

Head Bernoulli Equation in Process Engineering

Posted on February 9, 2024

Head Bernoulli is a term that refers to the total energy of a fluid at a given point in a steady flow system. It consists…

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

Vacuum Distillation of Atmospheric Residue

Posted on September 26, 2009October 28, 2012

In modern refinery practice the distillation of atmospheric residue is accomplished under high vacuum conditions in a specially designed tower whose internal equipment ensures a…

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…

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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
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

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