Safety and Pressure Relief
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Written by Milton Beychok
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Calculating the flow rates for accidental discharges can be confusing. Here, we'll discuss a standard set of equations for a variety of scenarios to help guide you through the process.
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Last Updated on Sunday, 09 November 2008 14:35 |
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Articles
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Written by Paul
Ostand
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Tank blanketing, or padding, refers to applying a cover of gas over the surface of a stores commodity; usually a liquid. Its purpose is either to protect or contain the stored product or prevent it from harming personnel, equipment, or the environment. In most cases the blanketing gas is nitrogen, although other gases may be used.
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Last Updated on Monday, 01 September 2008 12:18 |
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Articles
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Written by Phil
Leckner
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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 how temperature and backpressure affects the rupture disk specification and the relief pressure in the system. Part 5 discussed the Relief Valve/Rupture Disk combination. In this part, I conclude the series with a discussion of the rupture disk specification.
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Last Updated on Saturday, 16 August 2008 13:17 |
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Articles
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Written by Phil
Leckner
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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 how temperature and backpressure affects the rupture disk specification and the relief pressure in the system. In this part, I will discuss the Relief Valve/Rupture Disk combination.
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Last Updated on Saturday, 09 August 2008 14:43 |
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Articles
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Written by Phil
Leckner
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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 will discuss how temperature and backpressure affects the rupture disk design. Subsequent parts will include the Relief Valve/Rupture Disk combination, how to specify the rupture disk and some discussion on the type of rupture disks you can purchase.
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Last Updated on Saturday, 09 August 2008 14:26 |
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Articles
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Written by Phil
Leckner
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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. Subsequent parts will include temperature and backpressure affects, the Relief Valve/Rupture Disk combination, how to specify the rupture disk and some discussion on the type of rupture disks you can purchase.
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Last Updated on Friday, 08 August 2008 12:29 |
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Articles
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Written by Phil
Leckner
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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, the Relief Valve/Rupture Disk combination, how to specify the device and some discussion on the type of rupture disks you can purchase.
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Last Updated on Tuesday, 29 July 2008 13:55 |
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Articles
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Written by Phil
Leckner
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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 such as bursting pressure, tolerance, manufacturing range, etc., and discussions on the mechanical aspects that differentiate the various types of rupture disks, the seminar ended with many of those attending just shaking their heads. Most of the attendees just wanted to learn how to specify this item so the instrument engineer can buy one or the manufacturer can tell you what is needed.
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Last Updated on Sunday, 20 July 2008 10:34 |
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Articles
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Written by Phil
Leckner
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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.
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Last Updated on Sunday, 20 July 2008 16:16 |
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Articles
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Written by Phil
Leckner
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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.
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Last Updated on Saturday, 19 July 2008 17:41 |
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