Difference between revisions of "Importance of venting a processor"
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+ | ==introduction== | ||
+ | All GL reactors need to be vented to alow air to be displaced/replaced when oil/bio is added to or removed from the vessel. | ||
− | + | It is important that the vent doesn't have a valve on it as it '''must''' stay open at all times. | |
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− | + | ==Vent layout== | |
+ | The vent on a GL is normally on the vapor line after the condenser, this way any methanol fumes that are released during the reaction, or in the de-meth stage, will get condenced off and collected in the methanol collection vessel. | ||
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− | + | ==Concequences== | |
− | + | [[File:Collapsed processor 1.jpg|300x300|thumb|right|]] | |
− | + | If the vent becomes blocked it can produce a build up of possative or negative pressure. | |
+ | This can have sevear effects on the reactor it's self. | ||
+ | Negative pressure can and will cause the reactor to implode like in these pictures. | ||
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Revision as of 22:03, 30 January 2013
This page will soon be completed by Mark following an intensive and extensive wiki lesson.
Only if he was paying attention.
introduction
All GL reactors need to be vented to alow air to be displaced/replaced when oil/bio is added to or removed from the vessel.
It is important that the vent doesn't have a valve on it as it must stay open at all times.
Vent layout
The vent on a GL is normally on the vapor line after the condenser, this way any methanol fumes that are released during the reaction, or in the de-meth stage, will get condenced off and collected in the methanol collection vessel.
Concequences
If the vent becomes blocked it can produce a build up of possative or negative pressure. This can have sevear effects on the reactor it's self.
Negative pressure can and will cause the reactor to implode like in these pictures.
heading b
heading
Standard Cylinders | |||||
---|---|---|---|---|---|
British standard |
External diameter of cylinder (excluding insulation) |
External height over dome |
Min storage capacity | Expected port fittings | |
Direct | Indirect | ||||
mm | mm | Litres | Litres | female, BSP | |
0 | 300 | 1600 | 98 | 96 | 1" |
1 | 350 | 900 | 74 | 72 | 1" |
2 | 400 | 900 | 98 | 96 | 1" |
3 | 400 | 1050 | 116 | 114 | 1" |
4 | 450 | 675 | 86 | 84 | 1" |
5 | 450 | 750 | 98 | 95 | 1" |
6 | 450 | 825 | 109 | 106 | 1" |
7 | 450 | 900 | 120 | 117 | 1" |
8 | 450 | 1050 | 144 | 140 | 1 1/4" |
9 | 450 | 1200 | 166 | 162 | 1 1/4" |
9e | 450 | 1500 | 210 | 206 | 1 1/4" |
10 | 500 | 1200 | 200 | 190 | 1 1/2" |
11 | 500 | 1500 | 255 | 245 | 1 1/2" |
12 | 600 | 1200 | 290 | 280 | 2" |
13 | 600 | 1500 | 370 | 360 | 2" |
14 | 600 | 1800 | 450 | 440 | 2" |