next newest topic | next oldest topic |
Author | Topic: Thick Hips Sheet- STREAKS |
JamieMadronich Member Posts: 4 |
posted April 03, 2007 08:26 AM
Moisture or Degraded Resin??? We are trying to make thick HIPS sheet from recycled HIPS repro and regrind. The thicker we make the sheet the more problems we are getting with streaks caused by moisture or volatiles?? We can make sheet up to 0.080 with out much problem but it gets progressively worse on sheet up to 0.250 inch. We have a 3.5 inch two stage with a gear pump. Our extruder is vented with a properly funcitoning vacuum pump. We can also predry the material but I did not think that was necessary with HIPS if our extruder was vented.
------------------ IP: Logged |
Tom C Moderator Posts: 837 |
posted April 03, 2007 08:48 AM
Are you running the same process conditions for the different sheet thicknesses? What is the head pressure for the different thicknesses? What is the vacuum level you are getting? ------------------ Tom Cunningham www.ExtrusionTechnicalServices.com IP: Logged |
JamieMadronich Member Posts: 4 |
posted April 03, 2007 11:46 AM
We are getting a vacuum of between -15 and -20 in. Hg. We have tried the same conditions as with the thin sheet but we have also tried many other temp profiles and head pressures. We have tried different head pressures both by using different screen packs and by adjusting the suction pressure to the gear pump. Notes: Thanks a lot for your help.
IP: Logged |
Steve H Moderator Posts: 404 |
posted April 03, 2007 03:08 PM
G'day Jamie Welcome to the single screw forum. Is the streaking present at all when you are running thinner gauge sheet? While HIPS isn't hydroscopic, surface moisture on granulated scrap will give the problem you describe, so a drying trial is worth a try. Dust on/in regrind/repro, gives sheet a cratered appearance. Do you know the history and grades of regrind/repro you are running, is there any chance of it including Flame Redardent HIPS. Steve ------------------ If at first you don't succeed, skydiving is not for you. IP: Logged |
Tom C Moderator Posts: 837 |
posted April 03, 2007 07:39 PM
Iw would seem given the screen pack and grea pump that you are delivering the same quality of melt to the die. If these is moisture present it would seem it need to come out of the die in either case. If degradation were the issue, I would think the less restrictive die would give less problems. Can you see the defects exiting the die, or only afterwards? Translation - Could your downstream process be casuing the issue? ------------------ Tom Cunningham www.ExtrusionTechnicalServices.com IP: Logged |
Stephen J. Derezinski Senior Member Posts: 65 |
posted April 03, 2007 10:08 PM
Jamie-- I suggest that the higher rate needed for the thicker sheet has greatly lowered the time for vapor/moisture to diffuse out of the melt in the degassing channels of your screw. Hence, the gas passes with the melt. A greater vacuum may help. Also, better pre-drying may help, as suggested in a previous note. Also, be sure there is enough back pressure to properly keep the second stage filled so that it seals the degassing stage from the exit of the extruder. Conversely, if the back pressure on the extruder is too high, then the second stage will be quite full (if not flooded.) This will minimize the area for degassing and impede the release of all of the troubling vapor/moisture. A good math model of your extruder can help you set the pressure for your thicker product. Summary: At the higher rate, you may have reduced area and reduced time for gases to diffuse in your degassing stage of your extruder. This causes imcomplete degassing. ------------------ IP: Logged |
JamieMadronich Member Posts: 4 |
posted April 04, 2007 06:15 PM
Thanks for all the input: Replies to some of the questions: 2. Defects are coming out of the die. It is quite visible. It is definitely not a downstream issue. 3. Head Pressure, rates etc. 4.Streaking present on thin sheet... Its quite interesting but no it is not at all an issue running sheet in the 0.025 range. It is quite noticable in 1/8 inch and worse in 1/4 inch. 5. Dust etc. causing craters. We are actually getting a little of this but it is a different and tolerable problem. OK I know you are all dieing to know what happened today after we dried the HIPS in a dessicant drier for 10 hrs. before we ran.....SAME SURFACE APPEARANCE!!! What "idiot boy"( my new nickname) didn't do was verify that the vacuum was in fact getting to the vacuum port. There was a hunk of plastic lodged in a valve blocking the vacuum. I made the mistake of assuming we had vacuum to the port just because there was vacuum at the gauge in the pipe. (Of course a couple of our experienced operators didn't check either) Restoring the vacuum cleared up the problem within 20 minutes. Another interesting thing was that although predrying did not appreciably improve the appearance of the sheet it did dramatically stabilize the extruder. Also interesting is that it was not in fact surface moisture or the drier would have corrected it. This means we must have an awful lot of residual monomer or degraded plastic in the feed stock.
Regards, Jamie ------------------ IP: Logged |
Tom C Moderator Posts: 837 |
posted April 04, 2007 06:26 PM
Jamie, I don't want to pick on you too much, but usually all that vapor leaking out around the sides of the vent cap gives away the problem. ------------------ Tom Cunningham www.ExtrusionTechnicalServices.com IP: Logged |
Steve H Moderator Posts: 404 |
posted April 04, 2007 07:37 PM
Hey Jamie, cool that things are better and thank you for taking the time to keep us in the loop. I think the there may be a couple of things happening here- certainly some moisture, maybe some air entrapment issues. Could there be some "plate out" on the internal flow surfaces of your die- if the lines appear then fade out= moiture/volatiles, if they appear and stay/get worse= plateout on internal/die lips. What are the mechanical propeties of your sheet like, colour HIPS gets a real yellow cast if it's "cooked" by agressive processing parameters/repeated passes through an extruder. Steve [This message has been edited by Steve H (edited April 04, 2007).] IP: Logged |
JamieMadronich Member Posts: 4 |
posted April 05, 2007 09:26 AM
Tom, Its funny but there was not any noticble vapour leaking out around the vent while the vacuum line was plugged. Now,another change besides preheating is that I decided to use a reverse profile to really heat up the material before it got to the vent so it would degass better. Maybe I was running it too cold into the vent as well??? -hence no vapour leakage around vent cover??? I know in a perfect world I shouldn't change more than one thing at once but I had to get the order out in a hurry. Steve, I can't tell if we are cooking it terms of yellowing as it is black utility grade HIPS. The streaks are oval shaped and look like a bubble getting flattened as it goes through the chill rolls. It is all over the surface of the sheet and it does not come and go. The streaks are approximately 1/8 inch wide and around 1/2 inch long typically. What do you mean by "plate out"? I've heard the term but can't recall what it means.
Jamie IP: Logged |
Steve H Moderator Posts: 404 |
posted April 05, 2007 05:12 PM
G'day Jamie Plate out is a buildup of additive ingredient and/or degraded polymer on the screw, adaptors, die, chill rolls or sizing equipment. Once a build up starts, it gets worse, the longer you run. The line/marks these buildups cause, remain at fixed points across the sheet. Sometimes this will occur right on the lip of a sheet die, and you can scrape it off with a soft brass scraper (with care) and continue without shutting the line down. If the buildup is on an internal flow surface, shutting down, stripping everything down and cleaning is generally the best option. I have had some good results with chemical purges, but these usually only reduce the effect, and don't eliminate it. Steve IP: Logged |
All times are ET (US) | next newest topic | next oldest topic |
Powered by Infopop www.infopop.com © 2000
Ultimate Bulletin Board 5.45a