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Pressure Drop in Piping

Bernoulli’s Theorem

Posted on September 25, 2009October 28, 2012

It is customary to express the energy contained in a fluid in terms of the potential energy contained in an equivalent height or “head” of…

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…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

Heat Exchangers

Aerial Coolers Part 1

Posted on September 15, 2009October 28, 2012

Aerial coolers are often used to cool a hot fluid to near ambient temperature. They are mechanically simple and flexible, and they eliminate the nuisance…

Fractions from atmospheric and vacuum distillation

Atmospheric Residue

Posted on September 26, 2009October 28, 2012

This is the bottom product from the atmospheric distillation of the crude oil. Most crude oils are distilled in the atmospheric crude oil tower to…

LTX Units and Line Heaters

Fire Tube Sizing

Posted on September 16, 2009October 28, 2012

The area of the fire tube is normally calculated based on a heat flux rate of 10,000 Btu/hr-ft2. The fire-tube length can be determined from:…

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…

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…

Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

LTX Units and Line Heaters

Line Heaters

Posted on September 15, 2009October 30, 2012

As shown in Figure 5-2, the well stream enters the first coil at its flowing tubing temperature and pressure. Alternatively, it could be choked at…

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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
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