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Mechanical Design of Pressure Vessels

Separator Pressure Vessels Temperature Design

Posted on September 23, 2009

The maximum and minimum design temperatures for a vessel will determine the maximum allowable stress value permitted for the material to be used in the…

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…

Hydrates

Water Vapor Condensation Process

Posted on September 15, 2009October 28, 2012

One method of assuring that hydrates do not form is to assure that the amount of water vapor in the gas is always less than…

Gas Processing

Structured Packing

Posted on May 27, 2013May 27, 2013

A bed of structured packing consists of a bed support upon which elements of structured packing are placed. Beds of structured packing typically have lower…

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.…

Pressure Drop in Piping

Reynolds Number Piping

Posted on September 25, 2009October 28, 2012

The Reynolds number is a dimensionless parameter that relates the ratio of inertial forces to viscous forces. It can be expressed by the following general…

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…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

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…

LTX Units and Line Heaters

LTX Coil Temperatures Sizing

Posted on September 16, 2009

In order to choose the coil length and diameter, a temperature must first be chosen upstream of the choke; the higher Th the longer the…

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Recent Posts

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  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
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  • Cyclone Separator Capacity

Categories

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  • Gas Processing
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  • Heat Transfer Theory
  • Hydrates
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  • LTX Units and Line Heaters
  • Mechanical Design of Pressure Vessels
  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
  • Treater Vessels Sizing
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  • Two Phase Separator Sizing
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  • Type Of Devices
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