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This informative blog allows plastics professionals to discuss plastics training and technology. Brought to you by Routsis Training: the plastic industry's premiere training provider.

Sharp Transition In Rheology Curve…

After performing an In-Mold Rheology Test, one blog reader had this question…

Jason
When performing the in-mold rheology test, I noticed a sharp drop when reaching a specific shear rate. After this point, the viscosity stabilizes at the lower value for the remainder of the higher shear rates. What is the cause for this abnormal viscosity curve.
My Response
Although this seems strange, it is not uncommon. Since changing the injection rate causes a difference in the amount of material entering the mold during fill, this might occur when molding a part where the highest pressure losses occur near the end of fill. You might see a drop in pressure if the part thickness increases, and a rise in pressure when the thickness decreases at the end of fill.
Additional Thoughts
In most cases, you will see a smooth in-mold rheology curve.
-Andy

Converting ºC To ºF…

A technician called our office the other day and asked this question…

Steve
How do I convert 250 degrees Celsius to Fahrenheit?

My Response
This can be done using any calculator, the two basic equations are as follows:
(ºC x 1.8) + 32 = ºF
(ºF – 32) / (1.8) = ºC
Therefor:
(250ºC x 1.8) + 32 = 482ºF
Adversely:
(482ºF – 32) / 1.8 = 250
Additional Thoughts
One way to remember this relationship is 1 degree Celsius equals 1.8 degrees Fahrenheit plus 32 (since water freezes at 32ºF rather than 0ºC).
-Andy

Comparing Machine Capabilities…

This query came in the other day through email…


Emailer
Today, I moved a mold from one machine to another. The peak injection pressure was 1450 bar with a 0.6 sec. cycle time. On the second machine, I can only get 1.03 sec. injection time at 900 bar. I cannot fill the mold even though the maximum available pressure is 1800 bar.
My Response
It is likely that your new machine lacks the injection speed in cubic millimeters per second to fill the mold.
The best way to approach this is to first determine the ‘Shot Volume Factor’  for your two machines (see Understanding Shot Volume Factors… for more about this). This factor converts the movement of the screw into the volume it displaces (this is expressed in 

mm^3/s).

 
If you multiply this factor by the injection speed used in your old machine, you can determine the volumetric injection rate in mm^3/s or cubic millimeters per second. If you divide this result by the volume factor of the second machine, you can determine the approximate injection speed necessary on the second machine. This will allow you to accurately compare the injection capacity of the two machines.

Additional Thoughts
Many of the newer molding machines are now providing much more helpful information such as the volumetric injection rate and displacement as well as the actual pressure being applied to the plastic during injection, pack, and recovery.

-Andy

Time Required for Process Stabilization…

This question highlights a common point of disagreement within the molding industry…

M.
How long does process stabilization take, from set-up to first good parts?
My Response
With the explosion of SMED, Single Minute Exchange of Dies, there are many companies who have successfully reduced their changeover time to a matter of minutes or even seconds. Unfortunately, the startup time is not always as fast.
Generally speaking, most processes take around 5-10 minutes to stabilize. This typically occurs when the flow length and the ability to fill the mold is not significantly affected by the temperature of specific mold components. You can still shorten this time to stabilization by taking steps like the following:
  • Pre-conditioning the tool temperature before installing it into the machine
  • Pre-heat the hot runner system before installing it into the machine
  • Use insulation between the mold and the machine platens
  • Purge regularly when the machine is idle to help stabilize the melt temperature
High speed molding, and thin wall molding processes where you are processing with a much tighter window, stabilization can take up to 2 hours. When such a situation takes place, it is important to document the variations that take place and develop a time schedule to adjust for this. For example, if the cores take an hour to stabilize, then you might be have to use one 2nd stage packing pressure and 1st stage speed for the first 15 minutes, and then drop them down each 15 minutes until the process stabilizes.
Additional Thoughts
Always document the process using the process outputs. This will help you better determine when the process achieves stabilization.
For more on this, I recommend: Process Inputs vs. Process Outputs
-Andy

Understanding the Dynamic Load Sensitivity Test…

I got this request during the weekend…

Tim
I would like an explanation on how to perform a Dynamic Load Sensitivity Test on Hydraulic Molding Machines.

My Response
Although we have training courses dedicated to this topic, I will try to give a brief overview here:
The Load Sensitivity Test is used to determine how the injection flow rate is altered by changes in molding conditions – such as material viscosity.
To test a machine’s ability to compensate for changes in material viscosity, two shots are made under different loads. This is done by injecting one shot into the mold and one shot into the air.
The objective of this test is to compare the two shots and calculate the load sensitivity of the machine. This is expressed as either:
– A percentage of change per thousand psi hydraulic pressure
– A percentage of change per ten thousand psi plastic pressure
Additional Thoughts
For a webinar about machine, mold, and process evaluation… please review:
Practical Scientific Molding Techniques
For machine, mold, and process evaluation training and worksheets, please review:
The Intelligent Molder Series
-Andy