Author
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Topic: Processing of Poly Coated Packaging Material
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dripl Member Posts: 2 From:Mumbai, Maharashtra, India Registered: Jul 2004
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posted July 14, 2004 09:20 AM
Hi, We are currently ivolved in recycling & processing of Tetra Pak & other polycoated paper packaging waste materials. Usually these material contain 70% Paper , 25% Polyethylene & About 5 % Aluminium Foil. We are currently exploring possibilities of extruding such wastes in to Simpl "I" or "U" Profiles. Since Paper is basically cellulose fibre I thought this is an appropriate topic. Any suggestions on the above topic ar ewelcome.
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zabielski Senior Member Posts: 324 From:McHenry, IL USA Registered: Nov 2002
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posted July 15, 2004 07:12 AM
You ought to consider extruding this without a breaker-plate or screens, as they will clog up quickly. Use a narrowing (neck-in) die to increase your backpressure, then allow that transition to go into your I or U shape die head. However, to optimize your shape, you want to immediately pass it into a spray-water vacuum box (long water though), then PULL - not allow your extruder to PUSH. This is referred to as pultrusion. You will need a very strong - repete - a very strong puller. Nothing beats success - like SUCCESS. Keep us posted, eh? IP: Logged |
dripl Member Posts: 2 From:Mumbai, Maharashtra, India Registered: Jul 2004
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posted July 16, 2004 02:59 AM
Dear Sir,Thank you very much for your valuable suggestions. What kind of L/D ratio would be required in the Extruder? Should we look for any specific design of screw? Should we look at pelletizing with Twin Srew Extruder & Than Extruding the Profiles of Single Screw Extruder or Irthere a method to extrude these Profiles Directly.
quote: Originally posted by zabielski: You ought to consider extruding this without a breaker-plate or screens, as they will clog up quickly. Use a narrowing (neck-in) die to increase your backpressure, then allow that transition to go into your I or U shape die head. However, to optimize your shape, you want to immediately pass it into a spray-water vacuum box (long water though), then PULL - not allow your extruder to PUSH. This is referred to as pultrusion. You will need a very strong - repete - a very strong puller. Nothing beats success - like SUCCESS. Keep us posted, eh?
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zabielski Senior Member Posts: 324 From:McHenry, IL USA Registered: Nov 2002
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posted July 16, 2004 06:37 AM
I'd suggest you defer the screw design question to Tom Cunningham on this web site, as he is the one who can advise you. I would think though that a 32:1 L/D single screw extruder should work very well, and NO, don't subject the material(s) to another heat history by pelletizing (which also adds costs). The trick is to have a grooved feed section with a compression ratio of about 3.5 to 5 to 1. You essentially would grind up the material, assure that it's kept dry, then auger it into a very large surge bin. The bin would be slightly pressurized, and be off-set to the feed hopper. The delivery would be into a large hopper VIA an auger feed from the surge bin. Your hopper could be made from polycarbonate sheet, and have an air inlet, so you can blow a slight (very slight) amount of air towards the fill rate sensor. This keeps the sensor clean and prevents surges. Now, hook up you auger feed rates and latch them to a PLC so that your screw speed would sycronize with the feed augers, as you ramp speeds up & down. Where are you located? IP: Logged |
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