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  Extruder Bridging Up

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Author Topic:   Extruder Bridging Up
dk1
Member

Posts: 4
From:Iowa Park, TX USA
Registered: Oct 2002

posted October 25, 2002 09:55 AM     Click Here to See the Profile for dk1     Edit/Delete Message   Reply w/Quote
An adhesive resin we use is bridging up in our extruder feed throat.
The extruder is a 1.5" DS.
and is running at 108 rpm.
the feed throat temp is 330 F

Would the extruder be bridging up due to excessive sheer forces creating heat in the feed throat? Or is it that the screw can't feed the required amount and the resin is sitting in the feed throat for to long?

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Peter P
Senior Member

Posts: 61
From:Nottingham, Notts., U.K.
Registered: Jun 2001

posted October 25, 2002 10:37 AM     Click Here to See the Profile for Peter P     Edit/Delete Message   Reply w/Quote
330°F corresponds to about 165°C, which is very high for the feed throat and is probably about the softening point of your material. You need to cool your feed section more effectively - extruders usually incorporate a water cooled section at the throat with some way of monitoring and controlling the water flow. The heat build-up is probably due to the conduction of heat back along the barrel from the barrel heaters.

Regards,

Peter P

[This message has been edited by Peter P (edited 10-26-2002).]

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Steve H
Moderator

Posts: 386
From:Christchurch,New Zealand
Registered: Jun 2001

posted October 25, 2002 01:54 PM     Click Here to See the Profile for Steve H   Click Here to Email Steve H     Edit/Delete Message   Reply w/Quote
DK
Peter is completely correct, can you cool the feed throat? Ideally you would also bore and cool the screw for about 2 LD's past the feed throat as well, but at 1.5", doing this may weaken your screw- talk to DS about doing this and see what they recommend.

Steve Hodgson

[This message has been edited by Steve H (edited 10-25-2002).]

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dk1
Member

Posts: 4
From:Iowa Park, TX USA
Registered: Oct 2002

posted October 25, 2002 02:10 PM     Click Here to See the Profile for dk1     Edit/Delete Message   Reply w/Quote
Unfortunately, there is no way to cool the feedthroat without purchasing a cooling system. I don't think my company would go for that.
I figured that decreasing the first barrel zone temp. would do the trick. What do you think decrease 10-20 F?

I'm fairly new to adhesive resins, is there something I should know about them extrusion wise?

Thanks

dk1

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Steve H
Moderator

Posts: 386
From:Christchurch,New Zealand
Registered: Jun 2001

posted October 25, 2002 03:29 PM     Click Here to See the Profile for Steve H   Click Here to Email Steve H     Edit/Delete Message   Reply w/Quote
When does the bridging problem occur- Start up, after running awhile?

Trying various feed zone temps may help- are you drying the adhesive resin before extruding it-Maybe lowering the drying temp a little might help.

The cooling system is fairly simple and low cost (so long as your feed throat has a cooling gallery). Even just running a water supply through it and then dumping the water would help. If the casting isn't bored, encasing it in a fabricated box, through which water was circulated would.

Setting up a cooling system will certainly cost, but that needs to be balance up against the cost of lost production, off spec material shipped out, non delivery on promised dates etc etc. Suddenly a few dollars dosn't seem so bad

Do a search on your material suppliers web site, you should be able to locate a copy of their data sheet and processing instructions.

Steve H


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Tom C
Moderator

Posts: 737
From:Brodheadsville, PA USA
Registered: Jun 2001

posted October 25, 2002 09:43 PM     Click Here to See the Profile for Tom C   Click Here to Email Tom C     Edit/Delete Message   Reply w/Quote
A quick, cheap and dirty cooling system can be had by wrapping the lower part of the hopper and throat with soft copper tubing. Run tap water through it, and then perhaps drain into the water bath. This is an easy way to see if the problem is heat control in the throat.

Tom C

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Steve H
Moderator

Posts: 386
From:Christchurch,New Zealand
Registered: Jun 2001

posted October 26, 2002 02:09 AM     Click Here to See the Profile for Steve H   Click Here to Email Steve H     Edit/Delete Message   Reply w/Quote
You could also try playing compressed air round the casting- Just to prove the cause and then make a case for a long term solution.

Steve

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alpertl
Senior Member

Posts: 49
From:Dayville, CT USA
Registered: May 2002

posted November 04, 2002 04:54 PM     Click Here to See the Profile for alpertl   Click Here to Email alpertl     Edit/Delete Message   Reply w/Quote
quote:
Originally posted by dk1:
Unfortunately, there is no way to cool the feedthroat without purchasing a cooling system. I don't think my company would go for that.
I figured that decreasing the first barrel zone temp. would do the trick. What do you think decrease 10-20 F?

I'm fairly new to adhesive resins, is there something I should know about them extrusion wise?

Thanks

dk1



Depending on the process, lowering the Z1 may raise your feed throat temp.

No way to get a chiller on the puppy, eh?

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alpertl
Senior Member

Posts: 49
From:Dayville, CT USA
Registered: May 2002

posted November 04, 2002 04:57 PM     Click Here to See the Profile for alpertl   Click Here to Email alpertl     Edit/Delete Message   Reply w/Quote
quote:
Originally posted by alpertl:

Depending on the process, lowering the Z1 may raise your feed throat temp.

No way to get a chiller on the puppy, eh?

Also, the DS feed throat does not route the cooling to the front section that is adjacent to the barrel. In the past, I have cross drilled these and added extra cooling to the forward section of the feed (if your agglomeration is attached to the downstream side of the feed opening, this may help you).

You would, of course, need to be careful to not damage the casting.


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zabielski
Senior Member

Posts: 386
From:McHenry, IL USA
Registered: Nov 2002

posted November 05, 2002 07:12 AM     Click Here to See the Profile for zabielski   Click Here to Email zabielski     Edit/Delete Message   Reply w/Quote
Since you say the Company you'r with won't spend any money, try to simply measure the feed throat with a hand pyrometer carefully taped to the inside of the hopper. Now determine the melting temperature of your adhesive resin (the Vendor should give you this info., or you can run a DSC yourself).

Ideally, a way to control the feed temperature bridging is to core your screw out to about two feet and insert a cooling wand with the installation of a rotary union. Then you can cool the shank and feed segment jsut prior, at and around the feed zone.

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dk1
Member

Posts: 4
From:Iowa Park, TX USA
Registered: Oct 2002

posted November 05, 2002 01:25 PM     Click Here to See the Profile for dk1     Edit/Delete Message   Reply w/Quote
Thank you everyone for your input. I have a little update. I can't put my finger on the bridging problem. (resin, extruder speed, etc????)
I decreased my BZ1 and BZ2 temps 15 F.
This seemed to work.

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alpertl
Senior Member

Posts: 49
From:Dayville, CT USA
Registered: May 2002

posted November 05, 2002 03:59 PM     Click Here to See the Profile for alpertl   Click Here to Email alpertl     Edit/Delete Message   Reply w/Quote
quote:
Originally posted by dk1:
Thank you everyone for your input. I have a little update. I can't put my finger on the bridging problem. (resin, extruder speed, etc????)
I decreased my BZ1 and BZ2 temps 15 F.
This seemed to work.


Davis machines are notorious for poor feed section cooling, as there is no coolong jacket in the downstream side of the feed opening and the softer low melt polymers tend to stick to the section adjacent to the barrel.
What I have done is the past is to double cross drill this section and reroute the cooling exit side of the feed throat back through the these cross drilled holes before it exits.

As far as a chiller is concerned, you could set up a cost savings measure (and ISO 1400). We use a closed chiller loop for all of our machines with a mix of glycol, and our savings has been calculated on +150K gallons of water a year for 6 small line (all machines are smaller, the biggest being 1.25").

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rvmalik
Member

Posts: 3
From:Mumbai, M.S., India
Registered: Nov 2002

posted November 12, 2002 12:09 PM     Click Here to See the Profile for rvmalik   Click Here to Email rvmalik     Edit/Delete Message   Reply w/Quote
In India, the overheating problem whould have been solved by spending not more than 20 dollars (INR 1000/-)!!!

Immediately after the hopper throat, a hollow pipe jacket with 2 flanges at ends and a hole of nearly barrel OD bored in the side flanges can be slid on the barrel and welded in place with 2 drilled water cooling ports of say 3/8" BSP size. Cool water can be circulated through this jacket to keep down the temperature at feed throat below the softening point of polymer. The cooling jacket length need be approx. 2D long with an annular gap of approx. 3/4" all around the barrel for water to pass. It is cheap!!

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dk1
Member

Posts: 4
From:Iowa Park, TX USA
Registered: Oct 2002

posted November 12, 2002 12:29 PM     Click Here to See the Profile for dk1     Edit/Delete Message   Reply w/Quote
thanks to everyone's help, I solved the bridge up problem.
I misspoke about the extruder having a cooling jacket. Upon closer inspection there is a small copper line running to the feed section.

This wasn't that big of a deal now that I think about it. I didn't realize it before, but the resin we're using allows me to dump the temp. down to 250 F in the first barrel zone. That seems to have helped a lot. Also, the cooling water line that I thought didn't go to the feed section wasn't turned up all the way.

Thanks again

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