News | February 24, 2003

Do I Have Enough Cooling Lines In My Mold?

Do I Have Enough Cooling Lines In My Mold?

By Douglas M. Bryce

OVERVIEW

 Once the molten plastic is injected into the cavity image, it is allowed to stay there, under pressure, until it has cooled down and solidified enough to be removed from the mold. The plastic need not be totally cooled, just enough to allow ejection of the finished product without unacceptable distortion occurring to the plastic. This cooling is accomplished through the use of a mold temperature control system that is used to remove heat from the mold and maintain the correct mold temperature for the specific plastic material and product design being employed. In the following section we will examine the more common methods used to accomplish this feat.

 * Waterlines

The use of waterlines machined throughout the mold to allow water to flow through the mold is the most common method of controlling mold temperature. This is accomplished by drilling holes (1/8" pipe, 1/4" pipe, and 3/8" pipe are most common) across the various plates of the mold, as close as possible to the actual molding area of the cavity sets. (See the following drawing).

 

 Common Waterline Layout

Because of the accuracy required, the drilled holes are usually machined using a gun drill or deep boring tool. Then they are fitted with pipe threads which are used for connecting nipples, hoses, and/or quick-disconnect fittings. Hoses are connected to floor-mounted temperature control units, or to water manifolds which are normally mounted on the molding machine. Regardless of which system or device is used to maintain mold temperature, it must be emphasized that there should be no more than a ten (10) degree (F) difference between any two points of the cavity molding surfaces, either between two points on the same mold half, or between two points of both mold halves. Any more than 10 degrees (F) difference will cause excessive stress to be molded into the part and also will result in unbalanced plastic flow during the injection phase. The excessive stress is caused by differences in the cooling time required for hotter sections of the mold. These areas also shrink more than the cooler sections.

 - Control Units Versus Manifolds

 Control Units

If floor mounted temperature control units are used, a single unit should be used for each half of the mold. This eliminates the practice of using heated water from the first mold half to try to "cool" the second mold half, as is done when using only one control unit. 

 

Mold Temperature Control Unit

The unit has a set point which is determined by the user. Water is circulated through the unit and heated by the unit until it meets the desired set point. Then the water simply continues to circulate until it gets too warm, at which point the unit begins to dump the heated water and replace it with tap water until the desired temperature is reached. This process continues as the unit functions to maintain the desired temperature. The temperature of the circulating water is read through a thermometer mounted on the unit. Remember that this is only an indication of the water temperature and NOT the mold temperature. The mold temperature must always be measured by using a surface pyrometer on the cavity surfaces.

 Manifolds

 If water manifolds are utilized, the water flow is manipulated by throttling shutoff valves at the  connection points of the manifold. Each line can be controlled independently. The mold temperature is determined by the flow of the water through these valves, but must be measured by a surface pyrometer on the mold surface itself. In most cases, the manifolds are connected to a source of chilled water, usually at a temperature of approximately 50 degrees F. The manifold concept is based on a system that can control the mold temperature once it is established, but requires a slow and steady buildup as the metal of the mold absorbs heat from the injected plastic. The manifold system then depends on the continuous heat of incoming plastic to create a buildup of heat in the mold to provide the proper molding temperature. Once that temperature is hit, the manifold system can maintain it. However, this process may take an hour or two to level out and the molding parameters may have to be adjusted constantly while that is happening to ensure properly molded parts.. This creates a condition of having to "tweak" the manifolds during the first hour or so of production until the mold reaches the intended temperature.

 Another problem is that some molders utilize a colder mold for faster cycles and more profits. In fact, especially when molding crystalline materials, most parts require a slow cool down. This normally means a warm mold and long cooling cycles to create the highest level of physical strength in the final part. Cold molds will negatively affect the physical properties of a molded part, while warm molds will enhance those same properties. There are few situations where cold molds should be used. If manifold systems are in place there is a tendency for the molder to routinely lower the mold temperatures close to that available from the manifold system, which is usually around 50 degrees F. This may result in faster cycles, but can create a major quality problem if not understood and controlled.

  - Laminar Flow Versus Turbulent Flow

 There are two different types of flow that water can experience when traveling through a waterline of a mold: laminar or turbulent. The following drawing shows the differences between the two conditions. Both conditions will remove heat from the surrounding mold metal, but the laminar flow is not nearly as effective as the turbulent flow.

 

 Laminar Flow Versus Turbulent Flow

 Note that in the laminar flow diagram the water travels in separate layers. The layers nearest the outside are next to the mold metal and are in direct contact with the heat that needs to be removed. These layers move slowly (due to friction) and then transfer some of that heat to the faster moving inner layers. But the very center layer, which is moving fastest of all, receives no heat at all.

 In the turbulent flow model the water is constantly being tumbled and mixed. All of the water is in contact with the mold metal at one time or another and all of it is used to remove heat from the mold metal. This is the desired effect.

Reynolds Number

The creation of turbulence is a function of flow rate, waterline diameter, water viscosity, water temperature, and velocity of the water as it travels through the channels. Whether concerning laminar or turbulent flow, these conditions are characterized by a ratio known as the Reynolds number. Conditions causing a Reynolds number of 2000 or less will result in laminar flow. Ideal turbulence is found when conditions create a Reynolds number of 3500 or more. And, in between exists a transition area that fluctuates between laminar and turbulent flow.

 Determining the existing Reynolds number can be achieved by using the following formula:

                                                 R = 3160 Q / Dn

 where     Q = flow rate in gpm
               D = diameter of waterline (inches)
               n = water viscosity (centistokes), see Table  below

      Water Temp.(F)                     Viscosity (n)

                32                                            1.79
                            50                                            1.30
                            68.4                                         1.00
                            100                                          0.68
                            150                                          0.43
                            212                                          0.28

       Table  - Water Viscosity Versus Temperature

The most important answer we are attempting to find is the gallons per minute (gpm) required to produce a specific Reynolds number. The gpm is easily variable when all other conditions are fixed. So let's perform an exercise to make that determination.

First we must know the temperature of the water entering the mold. We'll use the temperature of 50 degrees F. Then we need to know the diameter of the waterline we are using. If we use a 1/8 inch pipe diameter, the actual drilled hole opening diameter (water passage) is 11/32 inch. Because we want to obtain turbulent flow we will use a specific Reynolds number of 3500 (that's the minimum we should have).

Remember our formulas is:   R = 3160 Q / Dn. By plugging in the numbers we have established above we arrive at:                                       

                                                3500 = (3160 * Q) / (0.34375 * 1.30)
                                                                                or
                                               
Q = (3500 * 0.34375 * 1.30) / 3160 
                                                                                or
                                                Q = 0.495 gallons per minute

Therefore, a flow rate of 0.495 gpm with water temperature of 50 degrees F, will create proper turbulence (3500) through a 1/8 inch pipe waterline. The formula can be adjusted for finding other items such as what Reynolds number should be expected using specified waterline diameters and flow rates, or what temperature water would be needed to create a specific Reynolds number. The important thing to realize is that there are variable conditions under which the ideal Reynolds number range of from 3500 to 7000 can be achieved. We should strive to maintain a Reynolds number of 5000, if at all possible, to ensure that we are providing proper heat transfer ability for the coolant being used to control the operating temperature of the mold.

You can easily detect whether or not a mold temperature is being properly maintained by noting the temperature difference between water going in and water coming out. Contrary to popular belief, there should not be more than a 10 degree (F) difference between the two temperatures. If outgoing water is hotter than incoming water, it actually means that there is still too much heat being retained in the mold and the water is not bringing it out fast enough. An ideal condition is that the heat is being removed as fast as it is being created, which would result in the water temperature being exactly the same going in as coming out. While this may not be entirely possible, there should be no more than a 10 degree F difference as noted above. And, assuming waterlines have been designed for proper Reynolds number, if the return water line is hotter it can be an indicator that a scale build up is occurring in the lines, or some other item is plugging the flow.

- Determining Location Of Waterlines

An easy statement to make is that the waterlines should be located as close as possible to the surface of the mold actually forming the molded product. While that is easy to state, usually it is not easy to accomplish, if at all. The reason is that drilled waterlines must follow straight paths, while most molded products have 3 dimensional qualities and are not flat and straight. In many cases, drilled lines are placed such that they surround the part as much as possible, but do not take the exact configuration, as shown in the following drawing.

 

 Improper Waterline Pattern

The round-shape cavity is surrounded by a square-shape waterline pattern. This is not efficient and will cause uneven cooling in the molded part due to the uneven location of the water being used to pull heat from the plastic. The uneven cooling will result in a tendency for the flat part to warp and bow as some areas cool down quickly while others cool at a slower rate. The following drawing shows a more accepted waterline pattern for this product.

 

 Acceptable Waterline Pattern

 

Here, the coolant follows a pattern that is much closer to the actual shape of the product being molded. In order to create this pattern, however, a complicated system of drilled and plugged waterlines must be created. This is expensive, and still does not form an ideal pattern. A better pattern may be the one shown in the following drawing.

 

 Better Waterline Pattern

In this case, the water flows in a pattern that very closely matches the shape of the product being molded. However, to incorporate this pattern requires a system of open-faced channels, connected together, and sealed with "O" rings to eliminate leakage. While this provides the most acceptable pattern, it is expensive to create and requires constant maintenance to keep leaks from forming and damaging the molded parts as well as the mold itself.

A further problem is that the steel used for making the mold must contain the high pressure initiated by the injection phase of the molding process, so the waterlines can't be too close to the cavity or they will create a breakthrough of the cavity steel. A rule of thumb suggests that waterlines be no closer than 1-1/2 times their diameter, but a safer rule of thumb states they should be no closer than a full 2 diameters from the cavity.

 

Waterline Distance To Cavity

As we have shown earlier the diameter is determined by what is required to provide the proper Reynolds Number value, but that does not mean there should only be a single waterline. If depth allows, additional layers of waterlines can be used.

Another factor to be considered when locating waterlines is that there are other items that make up the construction of the mold that may cause interference with the waterlines. For instance, there are bolts that are used to hold the cavity blocks in place. These come from behind the cavity blocks and might interfere with any waterlines running under these blocks. Also, ejector pins for the part and for the runner must travel through the B side of the mold, and these might interfere with waterline locations.

 

Waterlines And Interference Items

 It is critical that the mold designer lay these items out with two primary thoughts in mind: first, locate the cavity blocks as close as possible to the center of the mold (to minimize flow travel of the incoming plastic); and second, to locate waterlines as close as possible to the contour of the cavity image. These two concepts must be brought to bear on each other until a compromise is created which satisfies both requirements.

- Bubblers And Cascades

Sometimes it is difficult to get temperature control water located where it is needed. An example would be in the center of a deep metal core such as those used for making waste baskets. In those cases, specially designed components can be used. One popular component is called a "cascade" and is commonly referred to as a "bubbler", or sometimes a "fountain".

 

 Water Cascade (Bubbler)

In a bubbler, the cooling medium (usually water) comes from the main cooling channel, enters at the bottom of the bubbler, flows up through an inner tubular device, cascades inside the unit, and flows down through an outer tubular device, exiting back into the main cooling channel. This exiting water carries heat from the cascade unit into the main cooling medium.

- Cooling Pins

Another device is known as a "cooling pin" (sometimes called a "heat pin"). This unit works on the conduction principle and is made from a thermally conductive material such as beryllium copper. In the drawing that follows, the cooling pin is connected to the metal molding surface and the base of the pin sits in the main cooling channel. Heat is transferred from the plastic to the highly conductive cooling pin. The cooling medium takes heat away from the cooling pin by removing it from the base of the pin, to which point the heat has been conducted. In some designs, the pin is hollow and contains a liquid or gas that helps conductivity.

 

 Cooling Pin

Douglas M. Bryce
Chief Consultant
IPLAS
dbryce@iplas.com
http://www.iplas.com

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