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Mechanical Design of Pressure Vessels

Pressure Vessels Maximum Allowable Stress Values

Posted on September 23, 2009October 29, 2012

The maximum allowable stress values to be used in the calculation of the vessel’s wall thickness are given in the ASME Code for many different…

Potential Operating Problem

Foamy Crudes Problems

Posted on September 2, 2009

The major cause of foam in crude oil is the appearance of impurities, other than water, which are impractical to remove before the stream reaches…

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…

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…

Oil and Water Separation

Horizontal Three Phase Separator Part 1

Posted on August 21, 2009October 31, 2012

Three phase separator are designed as either horizontal or vertical pressure vessel. Figure 5-2 is a schematic of a horizontal separator. The fluid enters the…

Basic Separation

Separating Oil, Water, and Gas with Weir System Separators

Posted on February 9, 2024

A weir system separator is a device that separates a mixture of oil, water, and gas into its individual components. It is commonly used in…

Relief Valve Sizing

Orifice Gas Flow Rate

Posted on September 25, 2009October 28, 2012

The flow rate for gas through a given orifice area or the area required  for a given flow rate is obtained by:

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…

Separation

Stages Separation Selection

Posted on August 20, 2009October 29, 2012

As more stages are added to the process there is less and less incremental liquid recovery. The diminishing income for adding a stage must more…

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

  • 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

Categories

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  • Gas Processing
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  • Heat Transfer Theory
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  • 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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  • Shell and Tube Exchangers
  • Three Phase Separator Sizing
  • Treater Vessels Sizing
  • Two Phase Oil and Gas Separation
  • Two Phase Separator Equipment
  • Two Phase Separator Sizing
  • Two Phase Separator Theory
  • Type Of Devices
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  • Water Treating Theory
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