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by John Beaumont
The Beaumont Effect is recognized as the source of mold filling imbalances and product variations in molds
with four or more cavities. The worst failures caused by the phenomena can be most easily (visually) recognized
in molds with 8 or more cavities. However, shear induced melt variations impact every injection molded
part, with a greater influence than most realize….
Art Schubert of RJG discusses how to capitilize on the power of process simulation and building an injection molding process prior to building a mold.
Watch the YouTube presentation below for information about Plastic411.com ..
It is curious that in a world that relies increasingly on documentation, the attention to the details of polymer composition receive so little attention. Companies will fill volumes with procedures for various aspects of their manufacturing processes. However, no serious consideration is given to verifying the composition of the raw materials that are used to produce the various molded parts until there is a problem. Instead, there is a tendency simply to refer back to whatever published information is available from the material supplier….
By Garrett MacKenzie
Viscosity is a very large category that has huge effects on standardizing molding processes. It is also one of the most important factors in a molder’s arsenal of making process changes. This article will first explain viscosity, and then delve into different situations where viscosity may help or be hurting a processors goal of zero scrap and high output…..
By Garrett MacKenzie
When trying to establish process control in plastic injection, watering the tool is a key variable that is often overlooked. Water set-up and design are every bit as important as establishing and recording a repeatable process. The steps taken when watering a mold are key to a processor’s goal of consistency. If during the design and development stage, watering is put on the back burner as an “unimportant” variable, the potential for lost process control is huge.
Below are some insights into the most important facets of cooling or heating your mold, as well as what recordable data are important in the initial stages of process engineering…
By Garrett MacKenzie
I once had a plant manager who had the perfect analogy for the use of visual management, by implementing an engineered shop floor layout with clear and concise instructions at each employee’s workstation. The question he asked our team was this: “Why is it that when you look at a shampoo bottle, there are directions to ‘Rinse, Lather and Repeat’?” His answer was simple, yet thought-provoking. ”Someone at some point stood there with the bottle, trying to figure out what to do with it.”
Simply put, the better you are able to remove complexity from the shop floor and provide concrete visual and descriptive aids, the more control you will have over your plant’s overall performance…..
By Garrett MacKenzie: October 18, 2016
In lean manufacturing, changeover times are a vital component of shop performance. Minimal down time assures that multiple changeovers have little effect on a plant’s available machine time available. After all, less down time in the production equation offers more opportunities to take on more work and increase company profits. This article outlines specific approaches towards color changes that will support the potential of completing color changeovers in 3 to 7 minutes. This may seem like an impossible task to some, but with the proper planning, methods and equipment, it is an attainable and repeatable goal…..
By Garrett MacKenzie
The weekend comes to an end and the time comes to bring the molding floor back online for the beginning of a new work week. A molder can sometimes dread the tasks associated with a full plant restart. There are many potential failures that can occur as a plant is returned to a production state. Despite these risks, much of the headache can be avoided simply through proper shutdown and start up procedures. The following article addresses many key components that often lead to poor restarts. It also provides insight into some of the methods that can be implemented to not only reduce system breakdowns, but also can offer smoother start-ups with fewer problems.
Anyone who has experienced a full plant restart can tell you it can either be a smooth or a tragic event. As much as we wish that machines, tools and equipment would just cooperate, this simply is not always the case. It is important to understand the key components of start-up to be able to counter with fail-safe procedures on restart. Rushing through start-up often leads to failures within the facility. Here are some of the key components that lead to poor starts, as well as what you can do to prevent these factors from negatively affecting your shop:
Shutdown: One of the first key considerations to plant restart is shut down. Shutting your shop down is best viewed as preparation for plant start-up. Your facility’s shutdown procedures are one of the biggest contributing factors in how effectively your team brings the plant back into a new production workweek. Here are some of the primary focuses in plant shutdown:
1. Material Handling: There are many material-related failures that can cause poor starts. At shutdown, make sure your gaylords and material containers have been covered to prevent contamination and excessive exposure to moisture. Dried material in hoppers or one-shots above the press should be removed in anticipation of the restart, and to prevent wet material from being a start-up concern. As the press is shut down, run the barrel dry. This prevents material from bridging in the feedthroat of the press and causing unneeded downtime.
If dryers are to be left on over the weekend, their temperatures should be banked (lowered) to help prevent overdrying.
2. Tooling: Molds are a key focus. Improper shutdowns can be a primary reason for poor start-ups. Mold chillers are prone to sweating and should be cycled 5-10 minutes with the chiller off prior to full shutdown. This helps to reduce sweating, a primary cause of rust. Tooling should be cleaned and sprayed with rust preventative, and moving components should be inspected for wear and proper grease.
When working with clear polycarbonate or light colored materials and a hot runner mold, it is good practice to shut the hot runner off and allow the machine to cycle until the mold no longer produces parts. This keeps material from baking in the manifold, and reduces contamination at start up.
Mold should be left with mold halves touching (not under pressure) to protect the mold faces. Look for signs of water leaks on top of the mold. If they exist, fix the leak and soak up water to prevent it from getting inside the mold. Main water should be shut off and relieve the pressure from all water circuits.
3. Press Side: The barrel should be left empty, and the screw sucked back to about 1.00 to prevent drooling and to leave the screw in a neutral state. As mentioned above, mold halves should be left touching to prevent exposure to environmental exposure to moisture while in stasis. Check the bushing, purge tray and press bed for material to prevent unneeded downtime during start-up. The production area should be left clean, and ready for the team responsible for beginning the production week. Heats should either be banked at 300F, or you can perform a complete press power down, depending on your facility’s start-up approach.
Materials prone to degradation (such as nylon, acetal, ABS, etc.) should be purged out using a purging compound and/ or an inert material such as polypropylene. Verify that drying sources have either been set to banked (reduced) temperatures or have been powered down. Thermolators should be turned off, and the pressures on them released.
Make sure all auxiliary equipment is turned off, and that the production area has been prepared for the start-up team’s duties. Be sure to provide that team with a list of scrap / downtime issues that occurred during the last shift of the week, so the team’s members are fully aware of potential problems.
Press shutdown provides the perfect opportunity for a post-production preventative maintenance inspection. Tiebars, belts, hoses, oil levels, lubrication systems, etc. should be inspected for proper working conditions.
Molders, start your facilities
The key to a successful plant start-up is preparation. Clean starts are the result of careful planning and prudent procedures that prevent problematic production restarts. The following section addresses some of the primary focuses the start-up team should address prior to and during the start-up event:
1. Dryers: Plastics that require drying are a key consideration to address when returning the floor to production. Material moisture can wreak havoc on a start-up team’s goal of low scrap and fast and efficient restarts. If the dryer temperatures were reduced to a bank temp, then less drying time would be required to assure that material moisture is at an adequate state. If unsure what temperature to bank your dyer at, use the formula of 60% of actual drying termperature. It is important to note that not all materials require the dryers to be banked over the weekend. Best practice is to bank all dryers to assure that heat sensitive materials do not get overdried without the presence of material throughput.
Moisture content can be quickly and easily verified using a moisture analyzer. In addition, the first 25 pounds of material in the hopper should be drained due to poor circulation of heated air to the bottom of the dryer cone. As the material is drained, hold your hand in the path of the material exiting and drain until it is consistently hot to the touch. Do not load to the feed throat until just before you begin production.
2. Molds: Inspect the mold for signs of abnormal conditions or rust. Cycle the clamp a few times to inspect for proper operation and clamp set-up. Fully clean the mold and inspect any moving mechanisms or contact points to assure they are properly lubricated. If the mold is normally heated, then turn the water and thermolators on, allowing the tool to heat-soak with mold halves touching for about 15 minutes to ensure the mold faces are consistent in temperature.
Inspect water hook-ups for signs of leaking, and repair these to prevent moisture from being a cause of scrap. Also inspect core lines for excessive wear and/ or leaks.
Hot runner molds should be preheated and allowed to heat-soak. Check all water valves to assure they are in the “open” position and feel lines for turbulent flow.
3. Screw & Barrel: Make sure that the barrel has been brought up to temperature, and once temps have been achieved heat-soak the barrel for at least 20 minutes. Not doing so could lead to damage to the screw / barrel assembly. Review each temperature zone to assure that heater bands are working properly and each zone is at the required temperature. Watch for zones that do not come up to temperature at a normal rate in comparison to the zones around them. This can be a sign of a worn or damaged heater band.
The screw should be purged thoroughly prior to beginning the first cycle to assure that all purge compound and degraded material has been removed and that fresh material is what you will be shooting into the mold.
In closing, consistency in your shutdown/ start-up procedures cannot be stressed enough. All individuals assigned to these tasks should be trained to perform these duties uniformly. The more variance there is from press to press (or even job to job), the more likely that poor efficiencies and downtime will result. By incorporating standardized procedures in your shutdown, you improve your capability of solid starts. Your start-ups require a lot less thought and are stronger, with less scrap and a much smoother return to full production.