Sunday, January 24, 2010

Drop Test on PVC Profiles

Skippy - hey Buzz - here is another typical extrusion scenerio -

“Using ASTM D4495 to test rigid PVC profiles from extrusion. The problem I’m having is that very few of the profiles are failing . . .

The standard calls for room temperature conditioning, and when a 10 lb weight strikes the profiles, even from a height of 30 inches, no damage is done as far as failure, denting yes, no cracking . . .

I’ve even increased the weight to 14lbs and nothing. Any ideas”


Buzz - As the standard points out

(http://www.astm.org/Standards/D4495.htm),

results obtained by use of this test method can be used in two ways:

a) As the basis for establishing impact-test requirements in product standards, and or

b) To measure the effect of changes in materials or processing.

Skippy - isn't drop dart impact testing by profile extrusion houses done in foot pounds per mil (so two different wall thickness samples from the same materials would be subjected to different pass/fail drop heights/weights but the same overall criteria?)

Buzz - yes and is used to determine the limits of acceptable ductile or brittle failure modes - mention made above is that "only a few are failing". Actually at the maximum for acceptable failure mode - none should fail - perhaps the testing is at too high a standard to be appropriate (just beyond what would be "acceptable") or the testing isn't destructive enough if you are hoping for failure more often or every time?

Skippy - Additional questions requiring study come to mind given the presented information

- Are you testing for ductile or brittle failure
- is your calculation for inches of height per pound correct
- how long is the product resting between production time and testing
- would the application benefit or call for an annealing process involved to relax stress
- how thick is the product in mils
- what tup shape are you using
- etc

Buzz - Perhaps just as important, after the drop dart testing, are you giving it a more "real life" type 'whammo' testing - the kind of test when a worker punches through it with a nail, or drops it from the truck, or off a roof, in hot and more importantly cold weather; etc?

Also, we are assuming that dimensions and aesthetics are acceptable and accounted for in the testing at current (measured and reproducable) run conditions - aka you should be doing this testing to failure on parts that are in all other ways acceptable - if not, when or as you make additional changes, your test results may be suspect or worse, value-less.

Just our two cents -
Skippy and Buzz

Sunday, January 17, 2010

Extrusion of PETG - more thoughts

Skippy - hey Buzz - we never did actually give a "heat profile" to start up the PETG in the last discussion -

Buzz - yes, correct. Why? Well, mostly to see if these comments were helpful in the event that they did in fact have a start profile capable of

a) getting melt to the tooling and
b) keeping a steady state melt coming

No mention of the current melt temperature or current heat profiles or equipment, rates, tooling etc was given, (we are also assuming that adequate drying was in fact occuring) and PETG doesn't have too much in the way of "hot guts" anyway -

Skippy: so we pulled up a little short in the actual "heat profile" part of the answer on purpose since they didn't mention the equipment, screw/barrel etc being used. Suffice it to say that achieving the recommended melt temperature on heated (and controlled heating) screws and tooling is necessary; more information is required to make a more specific recommendation.

Buzz: Yes, much will depend on the screw length/diameter and screw design and intended rates and draw-down. The first couple of zones can be used to keep the melt cooler (but this again depends on screw design) and it is generally wise to keep barrel cooling OFF during start up to avoid freezing material along the screw and creating melt blockages.

Skippy: Typically, processors successful at extruding tubing and profiles from PETG use an "efficient" screw design to keep the melt and unmelt seperate until near the end of the transition area - particularly with thin re-granulated clean dry scrap. And generally (as indicated by Eastman) high compression screws like those designed for HDPE will generally not be suitable for PETG copolyester since excessive melt temperature and poor melt strength usually result -

Just our two cents
Skippy and Buzz

Wednesday, January 6, 2010

PETG tubing question

Skippy: Hey Buzz; Happy 2010!

Buzz: Howdy Skip - same to you. Glad to get 2009 behind us and start moving forward again -

Skippy: - right. To kick off the year - how about a quick processing question - the material? PETG or glycol modified PET for us extruders -

The question goes:
"Can anyone recommend a heat profile for extruding a PETG Tube 3" in Dia with a wall of 1 mm? Experiencing too much sag between the Die and the water tank in a vac sizer."

Buzz: the real answer of course is a heat profile that yields the correct clarity, and the least adhesive version of the material with the most hot guts you can get. This would of course also have to take into account the type of screw, compression, screens, tooling die pressure drop and other items. Not to mention that a heat profile while extruding at rate may or may not be the same as during string up, etc etc etc -

Skippy - well, yes, hopefully a dialog will ensue that will prompt a few more details. Do we have any thoughts that we can share assuming that the heat profile that is being used now is correct (and it just seems too hard to handle?)

Buzz: - you bet - although we can not be sure by the question as asked is whether we are asking in this way due to a surface issue, control of ovality or inability to string up. Will assume the worst -

There are a couple of more important questions for glycol modified PET -

1) What is the DRAW DOWN of the material - draw down orientation can be very useful; we used to produce our tooling approximately 50-80% greater than the size of the drawn down part for 'some' dependable orientation between the pin/shell and the calibration kiss.

2) Do you have an open air passage to the inside of the tube through the pins (perhaps through one or more spider legs) to allow air pressure inside the tube as you string it up?

3) is your tank in a position to give you the best shot at string up and running? Normally, you have the tank on center line in both plan and elevation to balance out "kiss", but this material is ADHESIVE versus just COHESIVE at correct melt temperature, so the KISS has to be at the last possible instant - you can’t just rub it all over and around the entrance of the sizing; it will want to set up too quickly, so you need a fair amount of draw down.

4) What is the nature of your calibration design - wafers, solid sleeve, rifled sleeve etc. as well as the surface texture - smooth, glass beaded, chromed etc.

Skippy: What about this "sag" business?

Buzz: At the same time as you are drawing down, the tube is wanting to "sag" due to gravity; recognizing, planning and depending on the "sag" that you mention for good clarity can be advantageous - so for this reason, the vacuum sizing tank as a whole is inline from a plan and elevation view as well as level for start up but after the string up, you will run it LOWER (still level; drop BOTH ends) than the die and backed away to point that still allows a kiss, but minimal contact prior to going down the "barrel" of the tubing calibration unit - and the tube does some controlled "sagging" as it falls from the die face down to a lower level calibration entrance level, then is pulled in evenly into the calibration unit.

Skippy - Cool; any more pointers?

Buzz: Assuming you are using a vacuum tank, I prefer a vacuum chamber that is 2' or less to get the line up into a tube quickly. Mount a fogging sprayer in the lid of the tank that can be used to spray the material with a mist of water (which will harden it pretty quickly at low speeds). You use this during the vacuum chamber sealing and water fill, then turn it off once a regular vacuum is achieved.

Skippy: What about gasketing?

Buzz: Be sure to have an adequate seal at the down stream exit of the vacuum chamber - one sealing material preferred is a silicone rubber (smooth orange) that is pretty friendly to sticky PETG. Use a few test swatches - you are looking for a supple material that will stretch to seal off as pulled downstream but doesn't stick and release. In general, the gasket material might ben1/8" thick and cut about 1/4-3/8" smaller on center than the OD of the final tube depending on suppleness. It is extremely important to cut the inside circle of the gasket on center with the supports and the tube itself. The seal material should be supported on BOTH sides of the seal with semi rigid to hard supports. The UPSTREAM support ring should be the OD of the tube plus a smidgeon (maybe 1/8" but not more than one thickness of the seal material larger than the final tube OD). Not larger than one times the thickness of the seal material, or the seal can be sucked upstream through the support easily. The DOWNSTREAM support ring should be the OD of the tube Plus 3 times the thickness of the seal material and a smidgeon more, so as not to be pinched too tightly by the tube when it is pulled round and the friction between it and the tube pulls it evenly down stream to minimize drag/release marks.

Skippy - gee the gasket and tube sealing technique described there sounds like a good practice on just about any tubing -

Buzz - Right!

In addition, you will need cooling that is MEASUREABLE in gallons per minute depending on line speed and calibration design for duplication in the future (see another post about water use across a plant), and a water level that has the cooling around the calibration deep enough to prevent air being cavitated into the cooling stream turbulence.

At string up, use a bit of silicone mold release on the shell and pin face that is clean to avoid material sticking to these surfaces and melting into "drool". Try to control your pin/shell temperatures to the extent that you can cool down the shell slightly to below the melt temperature which will result in a duller looking matte surface (melt fracture as the material slows down at the wall) at string up. This will give you a little more in the way of "hot guts" with a material that is very soupy at melt. When the Shell is a bit colder than the Pin, the material will bloom AWAY from the pin face once trimmed off. Spray a bit of silicone mold release on the pin face, then work to string up the line through the calibrator and avoiding touching the die face with the PETG as you pull it into the calibration towards the take off. Some of the sticky material may have stuck to the Shell face during the bloom once you get the line strung, you can scrape the face of the shell as necessary to clean up any material (being careful not to cut the material off the pin etc).

Skippy - is it hard to handle down line towards the take off?

Buzz: Once you are pulling the material down line, twist the material as you pull it into a 'rope" in water that has been brought up to the bottom edge of the calibration. The transition point is so abrupt that it will harden very quickly at this point; the twisting into the rope keeps it straight -

This next part is a little tricky - it takes a time or two to get the hang of it; read and visualize it a couple times before trials:

Once in the take off, you need to seal up the vacuum chamber -

a) move the tank forward to an adequate "kiss point", and
b) will open the drain to the chamber slightly (only a crack - this will help prevent pulling too much vacuum too quickly) and you
c) will apply vacuum to the calibration chamber, while you
d) turn the water misting/fogger lightly on (don't blow it out the face of the die) to set the tubing up as a "tube" while you simultaneously use a wet rag in the exit side seal area to "seal" the vacuum chamber around the rope until the "tube" arrives and is sealed with the gasketing. You do turn on the general fill water to be bring up the water level as well - just enough to fill but not flood out the front and hit the die - the light vacuum being maintained with the wet rag at the back and the drain cracked should allow you to make a "tube" in the sizer and keep water from going forward to the die -

Skippy: So . . . you want to be pulling enough vacuum to encourage the air pressure in the tube to expand it to fill the calibration unit and be raising the general water level to coincide with covering the tube when the mostly filled tube gets to the rear seal. Once you have good vacuum and the tube covered, close off the drain, bring your water level on up and level out your vacuum in the chamber?

Buzz: Perfect! Get things up to rate, drop your tank slightly and move the kiss back to a sweet spot and run with it.

These thoughts should get you up and running - good luck.

Just our two cents -
Skippy and Buzz