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Author | Topic: Venting gas from extruder |
felix Senior Member Posts: 59 |
posted March 19, 2003 12:39 PM
Hello everyone, Does anyone have any idea how to vent gas from the exit of an extruder, possibly through a valve of some sort at the exit of the extruder, in the adaptor? The situation is that the extruder shuts down, and the material inside the extruder develops vapor that has to be released due to safetly reasons. If a valve is used, there will be some melt flow I expect, but that's not a concern. Is this the best approach? IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted March 19, 2003 09:12 PM
Does this gas stay homogenized within the material (like during foam extrusion) or will it seperate out? Is this gas destructive (i.e. eat up barrel material, etc.)? Is this gas crucial to the extrusion, or a by-product of extruding this particular material? Most barrels have a rupture disc and perhaps you could adapt that, but it depends on what is going on... -Bob Cunningham IP: Logged |
Tom C Moderator Posts: 737 |
posted March 20, 2003 08:40 AM
Felix, I don't think you have any recourse except to purge the offending material out of the extruder when you shut down. Tom C IP: Logged |
Steve H Moderator Posts: 386 |
posted March 21, 2003 12:20 AM
Hi Felix What material are you extruding, and what sort of extrusion are you doing. Is the gas that's being given off a product of decomposion. Or is it the by product of an additive. How do you shut your extruder down? Steve H IP: Logged |
felix Senior Member Posts: 59 |
posted March 21, 2003 12:17 PM
quote: Hi Steve, the gas is given off as a result of an additive into the melt via an injection point mid way along the extruder. The gas should be there, but I am trying to install a safety device so that if power is lost, and the extruder shuts down, then this gas can be vented so as to not create a saftey hazard due to pressure buildup. Also, the gas is crucial to the extrusion process and seperates out of phase, and is not corrosive to the barrel/adaptor. Thank you for your help! IP: Logged |
Steve H Moderator Posts: 386 |
posted March 21, 2003 02:02 PM
Hi Felix In the event that power to the extruder is cut, will this also cut the gas injection system? My first thought is the latent heat in the die adaptors would allow the release of accumulated gas in the melt. So this shouldn't be a problem on shut down. There could be some problems restarting after power has suddenly been lost. You would want to reheat the line from either end toward the point at which the gas is injected, when the line is reheated. As Bob pointed out, burst discs(rupture plugs) should be fitted to relieve any extreme pressure build up. Replacing bolts on adaptors with studs and using brass nuts could be another option. Steve H IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted March 21, 2003 04:43 PM
Some extruders also are clamped to downstream with a 3-piece clamp that is tighened by a nut on a threaded brass rod- if the pressure gets too extreme, the threads will strip and the clamp will open just enough to relieve the pressure but the parts will stay captured (no flying dies). This is backup for the rupture disc. This is an emergency device only, but perhaps will provoke some thoughts to help solve your problem. -Bob Cunningham IP: Logged |
zabielski Senior Member Posts: 386 |
posted March 22, 2003 08:29 AM
I go along with Bob's last posting, as it does work well. Only other option that I can think of is to use a vacuum vented barrel, but you'd have to redesign your screw and allow for a devolitization point. The vacuum pump should then be water driven - as well. IP: Logged |
louis33 Senior Member Posts: 146 |
posted March 25, 2003 08:05 AM
Shouldn't your machine be equipped with a blow out plug? That being the case, if the pressure gets too high it should blow. SInce we are talking safty and then only in an emergency, you may want to install a second one in your head assembly. I'm not clear on the point about the gas being injected while the power is down, but I suppose that it could happen. IP: Logged |
felix Senior Member Posts: 59 |
posted March 25, 2003 11:09 PM
quote: The extruder has a rupture disc, it's actually a normal extruder that was adapted to insert an additive in the last 1/3rd of the barrel. The extruder is shut down periodically, and a valve closes the exit of the extruder which blocks off the entire flow rate. This is done to facilitate start up again. The blocking of the exit causes the gas to build up, and needs to be released. I think the best thing to do here is put a pneumatic to open a relief valve when the main valve closes to release the gas. This of course will release molten polymer as well, but that can be collected in a special stainless steel tank. Thanks for everyone's help! IP: Logged |
zabielski Senior Member Posts: 386 |
posted March 26, 2003 06:51 AM
Something to seriously consider with blow-off plugs. They are designed with sintered metal, and case harden within a year. Becoming case hardened, the designed pressure rating (i.e. 8,000 PSI) increases (i.e. 10,000 - 12,000 PSI) over the coarse of normal operating temperatures. You should replace them annually during a scheduled maintenance program. You can send out the old one to have it tested, and replaced. By keeping these records, you can then fairly estimate the point at which you should replace them - based on your operating temperatures. FLUKE has this service available, and it's a SAFE thing to do. IP: Logged |
louis33 Senior Member Posts: 146 |
posted March 26, 2003 08:13 AM
Are you sure about that? If that is the case, shouldn't there be a warning on them when they are purchased. This has me concerned as we depend on them to fail at the appropriate time. Is there some place where I can find more information? Thanks Louis IP: Logged |
zabielski Senior Member Posts: 386 |
posted March 27, 2003 07:14 AM
Yes, I'm sure about this. Check with your original equipment manufacturer. Sintered metals do this - just as brass does this when exposed to high temperatures for a long period of time. I poosted this as a concern for others due to an incident many years ago, when a flange blew off and the disc did not rupture. Fortunately, no one was injured, as I was heading up the Safety committee. There was no, and is no "warning", but there was a message in the instructions of installation stating (perhaps not in the exact words) that said something to the effect that "this device is subject to case hardening when exposed to high temperatures over a period of time." Perhaps it's time to check with FLUKE directly. IP: Logged |
louis33 Senior Member Posts: 146 |
posted March 27, 2003 08:37 AM
OK OK OK "Couldn't resist it Zeb" Thanks for that info. IP: Logged |
Tom C Moderator Posts: 737 |
posted March 27, 2003 09:11 AM
These posts are generally dealing with downstream addition in an extruder and saftey. I think a discussion of shutdown and startup of downstream addition extrusion process is in order. For normal startup and shutdown: 1) the first thing in the extruder, and the last thing in the extruder should be stable polymer. On shutdown all reactive, or potentially destrutive, components should be purged out, including easily degraded polymer. 2) When starting, once the screw, barrel, and die are full and extruding at full speed, then start adding other components in a logical order. (I prefer one by one.) 3) Dosing devices should have some type of positive shut off or injection screw to prevent polymer from flowing into the dosing device. 4) Dosing device interlocks should be considered which will not allow the device to operate unless conditions under #2 are being met. 5) A dosing extrution processes should go into an automatic shutdown procedure *before* any component of the formulation runs out, or if a dosing interlock trips.
1) As suggested proper setup of blow out plugs and die head clamps is a must. 2) It is possible that high pressures may be relieved out the throat of the extruder. 3) After some bad expereinces, I would generally recommend having a maintenance crew check out the extruder and dosing devices in order to bring them into a condition where thay can be restated in a normal condition, safely as described above.
[This message has been edited by Tom C (edited March 28, 2003).] IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted March 28, 2003 07:18 AM
And when starting/heating up, remember that polymer will expand. So, give it somewhere to go. In other words, don't heat up the screen changer or adapter pipe without heating the die, or you will get tremendous pressure in that adapter pipe because the polymer is trying to expand and has nowhere to go. (Yes, adapter pipes can explode)... -Bob Cunningham IP: Logged |
zabielski Senior Member Posts: 386 |
posted March 28, 2003 07:42 AM
Bob: Excellent advice! However, the original post was for "emergency" shut-downs. A redesign is needed here. The only alternative I can suggest realistically is to have an emergency Generator on stand-by. The problem however, is usually money and not common sense decisions. It does not sound like they want to really change anything significantly - and spend money on. [This message has been edited by zabielski (edited March 29, 2003).] IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted March 29, 2003 05:51 AM
I'm still trying to think of a solution for the situation as originally proposed. (I was just trying to add to the other note on general safety.) If you were able to tap a hole in the barrel for some sort of a pneumatic valve or something (assuming you could find one to handle the pressure), I would think you'd still have a dead spot where material would build up and burn, until it flakes off back into the flow and causes problems with the finished product. I really can't imagine a device that will allow pressure to be bled off. I can't think of another solution besides suppose the downstream equipment could be kept warm (using heater bands and an emergency generator) so that if the gas does expand, it just pushes material out through the die. -Bob Cunningham IP: Logged |
alpertl Senior Member Posts: 49 |
posted April 03, 2003 03:57 PM
quote: All of our machines have at minimum 2 transducers, with machine shutdown wired through the alarms. IP: Logged |
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