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Extrusion, Single Screw Information on Extruder Size versus Temp Profile Wanted
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Author | Topic: Information on Extruder Size versus Temp Profile Wanted |
StrapGod Senior Member Posts: 23 |
posted January 19, 2003 09:20 AM
I am looking for information concerning how temperature profiles may need tobe adjusted when extruder size is changed - same material - or output is increased substantially (10+ percent). I have a machine running polyester sheet and recently installed a new barrel and screw - we now have the capability of increasing output by 27% - as we head into that range, temperature profile is a question. Any help would be appreciated - thanks eveyone!! IP: Logged |
Tom C Moderator Posts: 737 |
posted January 19, 2003 10:03 AM
This is a great question. I would doubt if anyone could give you specifics as the relationships between material characteristics and extruder geometry is very complex and not all systems behave the same way. As a general guide you want to balance the pumping capacity of the extruder with the melting capacity. The setpoint for the process in order to achieve this are not intuitive, and this is why simulators were created. Simulators work great when they closely mimic the physical phenomenon inside the extruder. Fortunately in many cases they work well, as the most common behaviors are well know and studied. In some cases things happen inside an extruder which is different than the norm, and simulators have problems. If you are interested in seeing what a simulator predicts about this situation I would be willing to give it a try. First we need to verify that we can simulate the present condition. Please provide as much of the operating conditions, equipment description, and material information as you can. Typically you will need the permission of top management in order to release this proprietary information. If you can, I think it would be interesting for forum members to see. Tom C IP: Logged |
StrapGod Senior Member Posts: 23 |
posted January 19, 2003 10:26 AM
Appreciate the info TOm - I will discuss with my boss but I doubt that he would allow the release of this information. Thanks!! IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted January 19, 2003 12:45 PM
Mr. God, I don't understand- your topic asks about temperature changes with a change in extruder size, but then you say that you're using the same extruder with a new barrel and screw. Which is it? If your new screw is capable of 27% more output, is that because your old screw was very worn, or is the new screw a higher output (deeper) design? Other factors affect this too- I assume from your name that you are making strapping, presumably PP? Can your downstream equipment handle a 27% higher output? Not only the line speed of the converting equipment, but the higher pressure in the die, screenchanger, etc.? -Bob Cunningham IP: Logged |
StrapGod Senior Member Posts: 23 |
posted January 19, 2003 03:42 PM
I like that - Mr. God. Yes - I make strapping - PET however. I probaly made the original message aslightly confusing by mentioning extruder size and a change in screw and barrel. I am actually interested in both as I am running 2 different extruder sizes but using the same material - PET. In particular, I have just upgraded the screw and barrel on one of my lines due to screw and barrel being worn. The previous screw was not designed correctly and that is the primary reason for the 27% increase in output with new equipment. Downstream equipment not a problem. As I begin to slowly increase output beyond where we ever have gone before - the question arises concerning the temperature profile within the extruder. 20+ % decrease of time material is in extruder is substantial - not being a polymer engineer - I do not know the effects. Honestly, I am thinking temps need to go up. Thanks!! IP: Logged |
Bob Cunningham Senior Member Posts: 115 |
posted January 20, 2003 01:28 PM
It's hard to know exactly what's going to change without knowing the specifics of the old & new screws. But if I had to guess, I would think that the new screw is going to be deeper to give you the higher rate. A deeper screw means less shear- less shear means less heat. Less heat *might* mean that you'll get unmelted material through the end of the screw. If this happens, then you'll have to bump up the extruder heats to compensate. If this doesn't happen and a cold melt has no other bad effects on your process, then you can take your 27% more material and be happy! One other thing to watch is the melt pressure. If the melt is colder, your viscosity will increase, meaning you'll have higher pressures. If you were running quasi-high pressure before, it will really be high now! Not to mention that the higher rate alone will also give you higher pressures (takes more pressure to force more material out of the same die). If the higher pressures also cause no problems, then you are golden. -Bob Cunningham IP: Logged |
marko Member Posts: 2 |
posted February 24, 2003 11:17 AM
We also changed are screw giving us an 18% increase in output,Bobs comments on deeper screw flights & the effect on temperatures are correct. We found we had to increase the temps throuhout the barrel because of the decreased residence to time of the material. In are experience, a good target to aim for is to get your melt temp & die pressure the same as your old screw then do some running r&d
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