Between the Lines      
  November 2008 a newsletter from BE      
         
 

Increase output; make new products by retrofitting existing line.

     
 

 

Are you a film producer looking for ways to increase your output? Are you looking for methods of handling new materials and producing new downgauged (thinner) films? Is gauge control an issue? Do you want to wind larger rolls to reduce roll handling? The BE team can help. Our sales, service and engineering staff can help you identify new components for your existing blown film lines to help you with these issues.

Jim Stobie, Vice President of Sales North America says that in the US some monolayer film producers are moving up to three-layer lines. They want to use their existing downstream equipment but need to replace their die and add new extruders. “We have designed a compact three-extruder and die unit that can fit in a similar space to a monolayer line.This effectively allows the customer to move into new markets without investing in a complete new 3-layer line.”

To help a customer produce a new product Mark Wodrich, Area Sales Manager in the US worked with the customer to improve output rates and ensure thickness uniformity.his project involved install a new, more efficient air ring and add gusseting to their haul off. A new air ring has significant effect

In other situations when processors want to improve their output, the BE sales team can help you specify the size and type of extruder(s) needed. We can recommend the appropriate cooling hardware: air ring, IBC, blowers and coolers.

Improve thickness uniformity of films with BE I-Flex system can significantly reduce resin consumption—in some cases, by as much as 3%. Many film markets now require much more stringent gauge uniformity and we are poised to be able to provide the control required.

Converters are continually looking for ways to improve the efficiency of their processes. By winding larger rolls you will have fewer splices and reduced roll handling. These translate into efficiency of materials by generating less scrap and of labor by reducing material handling.  A 40-inch OD roll will have 78% more footage than a 30-inch OD roll, and a 60-inch OD roll will have 125% more footage than a 40-inch OD roll. Buying a new winder can generate the efficiency improvements converters need.

New materials demand new winding capabilities. The improved properties of new resins have allowed processors to downgauge films. These thinner films require more sensitive and sophisticated web handling equipment, especially if they are going to be wound into larger rolls. BE winders and other downstream equipment are designed to handle these new thin films.

If you want to change your product, make new products, increase your output and improve gauge uniformity call BE for retrofitting part of your line to achieve your desired results.

 

     
 
     
         
  Troubleshooting blown film processing - Part Three      
 

 

Diagnosing gels, unmelts and degraded gels.

 

Gels are often encountered in extrusion. In multilayer coextrusion you have to identify the source layer of the gels.

The causes of gels range from resin contamination to process issues to screw and die design. Depending on the causes of gels, they may have very different characteristics. You first need to deterimine if you have gels or unmelts.

Unmelts are not really gels by definition; rather, they are materials that have not been melted, hence, they are called unmelts. The easiest way to distinguish between gels and unmelts is to use a hot-stage microscope. The idea here is to see whether or not the gel will melt at a reasonable temperature, and if the temperature is within the range of the melting point of a known polymer. This would roughly identify the type of polymer (for example, PE or Polyamide), and therefore the source layer or layers of the unmelts. When the gel will not melt within a reasonable temperature range, then it is most likely a true gel. The use of Fourier Transform Infrared Microscopy  (FTIR) will then be required.

If a gel is identified as an unmelt, take a look at your resin sources, conveying system and blending system to rule out any potential resin contamination in these areas.

The next step and the most important; investigate the material’s processing temperature to ensure that all temperature zones are functioning properly and controlling to the preset target temperature on the recipe settings. Often a simple change in the barrel conditions of the extruder will significantly eliminate or reduce the number of unmelts. A basic understanding of the screw design would help with the extruder barrel zone temperature settings. There are basically three functional zones in a screw regardless of whether it is a single-stage compression screw or a barrier screw. They are named feed zone, melting zone and metering zone. All the melting of the polymer should take place before the start of the metering section. Too slow a melting rate results in an incomplete melting process; too fast a melting rate causes a premature solid bed breakup. Both contribute to the generation of unmelts.

Watch for resin blend compatibility. If changing the temperature profiles cannot eliminate unmelts completely, check into each component in the blend and determine how they interact with each other.

Screw design. If the steps described above fail to eliminate the melts you may have to explore a different screw design.

Degraded Gels

When gels are degraded or crosslinked, these gels will not be melted. In severe cases, they show up discolored from yellow to brown, or black.

Again, resin contamination is a possible culprit. Occasionally, foreign fibers in the resin cause a gel-like appearance. Normally, the use of Fourier Transform Infrared Microscopy (FTIR) will identify the foreign substance. Excessive processing temperatures can also contribute to premature degradation of the polymer.

Screw and barrel conditions. If the screw or the barrels are not in good working condition and are worn, the residence time of the materials in the extruder will increase dramatically. This would contribute to unexpectedly high melt temperatures. A variable depth thermocouple can help determine the temperature gradient in the melt stream, and indicate the true melt temperature. A fixed thermocouple only gives the melt temperature at the wall of the adapter, and may not indicate a true melt temperature in the middle of the melt stream.

Screw design. A poor screw design could contribute to potential degradation area.

Die design. Similarly, a poor die design could cause areas of unusually long residence time, which would contribute to polymer degrading in the die.

                           

In summary, to deal with gels you need to find the source layer of the problem; identify the material; determine if problem is a gel, unmelt or degraded gel. You do this by looking at resin blend compatibility, resin contamination, screw and barrel conditions in addition to screw and die design.

In the next issue of Between the Lines watch for our troubleshooting story on interfacial instability.

 

     
 

 

     
 

The Benefits of Streamlining in Die Design

     
  Streamlining can be defined as minimizing the resistance of a shape to the flow of a fluid. The first airplanes for example, were all but streamlined.      
 

 

Their designs were boxy, their shapes irregular and their surfaces rough. Among other things, they had exposed engines and fixed landing gear that added tremendous drag during flight. As a result, they could not fly very fast, their fuel efficiency was terrible, and their maneuverability was lacking.

     
 

Nowadays airplanes are much more streamlined, with smoother shapes and surfaces, and features like retractable landing gear. Fighter jets are the most streamlined of all airplanes because of the need to minimize drag to maximize speed, efficiency and maneuverability.

Many years ago BE realized the importance of streamlining and incorporated its principles to the development of its SCD® (Streamlined Coextrusion Die).  The SCD® is designed to minimize the resistance it imparts to the flow of melt through its distribution channels and spirals.

 

If streamlining brings to the airplane design the benefits of speed, efficiency and maneuverability, it brings to die design the benefits of low residence time distribution (RTD), efficient purging, and greater processing flexibility.

In our next issue of Between the Lines we will explain RTD and how streamlining affects it.

 

 

     
         
         


 

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