Latest Downloads
-
Refinery Tankageankur2061 - May 10 2012 08:07 AM
-
Minimum Safe Flow for a Centrifugal Pumpankur2061 - Apr 27 2012 06:56 AM
-
Natural Gas Boiler CalculationsSadananda Konchady - Mar 29 2012 06:55 PM
-
Hydrate Formation Temperatureankur2061 - Feb 29 2012 09:26 AM
-
Compressor Surge and Anti-Surge Controlankur2061 - Feb 21 2012 05:01 PM
-
Crane Fluid Flow Examples in MS Excel 1.11Art Montemayor - Jan 31 2012 08:22 PM
-
Surface Tension of Pure Liquidsankur2061 - Jan 24 2012 02:43 PM
-
Filament Yarn Quench Air Systemankur2061 - Jan 18 2012 05:03 PM
-
Gravity Tank Drainage Calculator for Uniform Cross Sectionsstudent88 - Dec 19 2011 03:16 PM
-
Gravity Tank Drainage Calculator for Hemispherical Cross Sectionsstudent88 - Dec 19 2011 03:14 PM
Popular Store Titles
Tank Jacket Calculator
Specification Sheet Collection
PIPESIZE
Relief Valve Sizing
Rupture Disc Sizing
Chemical and Process Engineering Resources
Safety and Pressure Relief
Relieve Valve Set Pressures
Nov 08 2010 06:30 PM |
pleckner
in Safety and Pressure Relief
As the title of this column implies, I intend to present various topics related to Process Engineering Design based on my knowledge and experiences. I will convey what approaches I think you should be taking. I will stress "the correct way" so don't ex...
Read story → 0 comments




Pyrophoric Iron Fires
Nov 08 2010 06:40 PM |
Mukesh Sahdev
in Safety and Pressure Relief
At one time or another, most refineries experience spontaneous ignition of iron sulfide either on the ground or inside equipment. When this occurs inside equipment like columns, vessels, and tanks and exchangers containing residual hydrocarbons and air...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 6
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
Part 1 of this series on rupture disks for Process Engineers covered why you use a rupture disk and when you might want to use this device. Part 2 discussed how to size the rupture disk. Part 3 discussed how to set the burst pressure. Part 4 discussed...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 5
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
Part 1 of this series on rupture disks for Process Engineers covered why you use a rupture disk and when you might want to use this device. Part 2 discussed how to size the rupture disk. Part 3 discussed how to set the burst pressure. Part 4 discussed...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 4
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
Part 1 of this series on rupture disks for Process Engineers covered why you use a rupture disk and when you might want to use this device. Part 2 discussed how to size the rupture disk. Part 3 discussed how to set the burst pressure. In this part, I w...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 3
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
Part 1 of this series on rupture disks for Process Engineers covered why you use a rupture disk and when you might want to use this device. Part 2 discussed how to size the rupture disk. In this part, I will cover how to set the burst pressure. Subsequ...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 2
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
Part 1 of this series on rupture disks for Process Engineers covered why you use a rupture disk and when you might want to use this device. This part will discuss how to size the rupture disk. Subsequent parts will include how to set the burst pressure...
Read story → 0 comments




Rupture Disks for Process Engineers - Part 1
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
This is a real story. A rupture disk manufacturer presented a seminar to a group consisting of junior and more senior level process design engineers (yours truly included) with a few instrument engineers thrown in. After about an hour of hearing terms...
Read story → 1 comments




Relief Valves: "What Can Go Wrong" Scen...
Nov 08 2010 06:40 PM |
pleckner
in Safety and Pressure Relief
What can go wrong in a chemical facility? Plenty! A report in the August 2000 issue of CEP1 shows that operator error or poor maintenance was the leading of cause of accidents for unfired pressure vessels eight years running. The ProblemAccidents not o...
Read story → 0 comments






FB