Melted cheese-like flow -- What is it called and its cause?

Click For Summary
SUMMARY

The discussion centers on the phenomenon of "stringy flow" in melted plastics, likened to melted cheese, and its relation to polymer rheology. Key terms include "laminar flow," which describes how polymers flow side by side, and "viscoelastic flow," which is influenced by molecular weight and poly-dispersivity. The string cheese effect, or de-lamination, can result from excessive heat, moisture, or shear rates during processing. Participants emphasize the importance of understanding polymer characteristics, such as additives and molecular weight, to mitigate these effects.

PREREQUISITES
  • Understanding of polymer rheology
  • Knowledge of viscoelastic flow properties
  • Familiarity with injection molding processes
  • Basic concepts of molecular weight in polymers
NEXT STEPS
  • Research "polymer rheology" for a deeper understanding of flow behaviors
  • Explore "viscoelasticity in polymers" to grasp its impact on processing
  • Investigate "molecular weight effects on polymer properties" for practical applications
  • Study "de-lamination in thermoplastics" to identify causes and solutions
USEFUL FOR

This discussion is beneficial for polymer scientists, materials engineers, and professionals involved in plastic processing and manufacturing, particularly those focused on optimizing polymer flow characteristics.

thepopasmurf
Messages
73
Reaction score
0
There are some plastics I am using that when melted, pull apart in a stringy way. My best comparison is like melted cheese in a sandwich.

I want to know more about this, but other than looking up 'polymer rheology', I'm not sure what I should call this type of flow. I want to know what causes it and if the molecular weight of the polymer is important.
 
Engineering news on Phys.org
Thermoforming. Vacuum forming. https://en.wikipedia.org/wiki/Thermoforming
The string patterns form when unsupported thinner areas heat and soften more rapidly, then merge with the nearby string of cooler material.
 
Is this the effect?
Partially degraded polymers (i.e. - an mixture of monomers and longer chains) often have this property.
High tack polymers tend to be stringier. Exxon Escorez and other tackfier additives can be blended with other polymers to enhance this effect.
 
  • Like
Likes   Reactions: Nidum
@Asymptotic, this effect seems close to what I am looking for. The wikipedia entry doesn't give much to build on, I guess 'stretching' and 'fingering' are the best things to look at.
 
In general it is non-Newtonian fluid flow . Most commonly encountered as visco-elastic flow though there are several other interesting variants .
 
  • Like
Likes   Reactions: RheologyIsFun and Chestermiller
The degree of viscoelasticity increases with increasing molecular weight and poly-dispersivity.
 
  • Like
Likes   Reactions: RheologyIsFun
Hey PopaSmurf,

A little more information is needed here such as the type of polymer you are using and is it glass filled, does it have lubricants or other additives?

The term for that type of flow is "laminar flow" and all polymers flow this way. essentially you have long polymer chains flowing side by side like two sheets of paper. There is no such thing as turbulent flow in plastics.

Molecular weight is very important in plastics as it dictates the quality of stiffness in the plastic as well as other properties. It will also give you an idea of how hard your polymer is to "push" (what pressures will I need to inject).

The string cheese effect you are describing sounds like de-lamination. This can be caused by degrading the material (temperatures are too high in the barrel or in the dryer), too much moisture being in your material or too high of a shear rate (injecting too fast).

I hope this helps!

Husky
 
MTU_Husky said:
Hey PopaSmurf,

A little more information is needed here such as the type of polymer you are using and is it glass filled, does it have lubricants or other additives?

The term for that type of flow is "laminar flow" and all polymers flow this way. essentially you have long polymer chains flowing side by side like two sheets of paper. There is no such thing as turbulent flow in plastics.
This is not correct. It is easily possible to achieve turbulent flow for polymers with low degree of polymerization.
 
  • Like
Likes   Reactions: RheologyIsFun
Chestermiller said:
This is not correct. It is easily possible to achieve turbulent flow for polymers with low degree of polymerization.

I definitely misread the original post as I thought they were referring to injection molding plastic but after re-reading it they just stated this happens when melting the plastic. Do we know what method/process they are using to melt?

It will not let me update my original post so I will correct it here. There is no turbulent flow in injection molding thermoplastics and the reason I say that is because I have calculated the Reynolds number for several different polymers using a fill velocity of 400 in/s and the highest Reynold value I can calculate is around 160. The crazy part is I am using relatively low viscosity (about 5 - 10 poise taken from a viscosity vs. shear rate curve at 80,000 1/s), a 0.06" gate diameter and an extremely fast injection speeds (the fastest I have ever worked with is 35 in/s and I am using 400 in/s in my calculations), which all should raise my Reynolds number vs normal operating conditions.

I would be interested to see a polymer process where they would see turbulent flow. What industries and processes use these polymers and what does the turbulent flow achieve for them? If you have a generic or trade name I would be interested in comparing to my industry.
 
  • #10
MTU_Husky said:
I definitely misread the original post as I thought they were referring to injection molding plastic but after re-reading it they just stated this happens when melting the plastic. Do we know what method/process they are using to melt?

It will not let me update my original post so I will correct it here. There is no turbulent flow in injection molding thermoplastics and the reason I say that is because I have calculated the Reynolds number for several different polymers using a fill velocity of 400 in/s and the highest Reynold value I can calculate is around 160. The crazy part is I am using relatively low viscosity (about 5 - 10 poise taken from a viscosity vs. shear rate curve at 80,000 1/s), a 0.06" gate diameter and an extremely fast injection speeds (the fastest I have ever worked with is 35 in/s and I am using 400 in/s in my calculations), which all should raise my Reynolds number vs normal operating conditions.

I would be interested to see a polymer process where they would see turbulent flow. What industries and processes use these polymers and what does the turbulent flow achieve for them? If you have a generic or trade name I would be interested in comparing to my industry.
I wasn't talking about any particular process. I was just saying that it is possible for polymers to exhibit turbulent flow.
 

Similar threads

Replies
0
Views
2K
  • · Replies 8 ·
Replies
8
Views
9K
  • · Replies 8 ·
Replies
8
Views
6K
  • · Replies 48 ·
2
Replies
48
Views
5K
  • · Replies 3 ·
Replies
3
Views
19K
  • · Replies 6 ·
Replies
6
Views
2K
  • · Replies 35 ·
2
Replies
35
Views
4K
  • · Replies 4 ·
Replies
4
Views
3K
  • · Replies 48 ·
2
Replies
48
Views
6K
Replies
5
Views
3K