A colder injection mold doesn’t always result in colder part temperatures

Sprue injection molded partHow many times have you heard someone say that the water temperature was turned down on the mold to run a faster cycle? The general assumption is that the colder you run the mold coolant temperature, the faster the part will cool, shortening the cycle time. After all, time is money, so the faster you can produce good quality parts, the more profitable your company will be. 

But we need to ask ourselves: How low can you go with water temperature before it has a negative effect on part quality and cycle time? For years, I have heard that lowering coolant temperature is only effective to 50°F. I have been taught this rule throughout my many years of molding, but I never saw any data to actually back up this theory. 

I recently found myself at a customer facility, and they were discussing a project that needed to reach a cycle time of 18 seconds on an eight-cavity PVC part. They informed me they were currently running a 22-second cycle with a water temperature of 50°F and were planning on sampling the mold with a water temperature of 32°F so they could lower the cycle time. I informed them of the theory that cooling was only effective to 50°F. The first question they asked me was: Do you have any data to back up the theory? Since I did not have any data, we decided to complete some testing to see if this theory was valid or if we could actually make cooler parts with coolant temperature below 50°F.

The first step we took was to select two molds that run in different machines to give us multiple processes from which to collect data. We started up the machines and observed their standard processes. While observing the processes, I learned that they remove the parts from the mold and then put them in a water tank to further cool the parts before they trim the cold sprue. If they cut the cold sprue off when the part is fresh out of the mold, there would be gate discharge, because the center of the part was still molten. This is when we decided to cut the sprue fresh out of the mold and use a pyrometer with a thin probe to check the internal part temperature. We found that the internal temperature for part A was 195°F and part B was 285°F. We then used this data to compare part temperatures from the other experiments we ran.

The importance of turbulent flow

I started looking at other production processes to observe the coolant going to each of the molds and found they had not checked for turbulent flow in either of these processes. For efficient cooling, it is important to have turbulent flow instead of laminar flow. In order to check for turbulent flow, you will need to use a flowmeter and the calculation listed in Figure 1 to determine the Reynolds number (RN). You will also need to look in the chart in Figure 2 to find the kinematic viscosity (KV) of the fluid you are using in your coolant system. A Reynolds number greater than 5,000 tells you that you have turbulent flow, whereas a Reynolds number below 5,000 tells you that you have laminar flow.

Reynolds number calculation
Figure 1. To check for turbulent flow, you will need to use a flowmeter and the calculation shown here to determine the Reynolds number.

During the initial investigation, I found that they were using a 50/50 water and ethylene glycol mix. When you use a 50/50 water and ethylene glycol mix, it can take up to three times the flow rate in order to achieve turbulent flow. When we tested both molds, the Reynolds number was found to be below 3,100 RN, therefore I knew that they did not have turbulent flow going through their molds. We decided to run straight water through their portable chiller to see if we could achieve turbulent flow. The first thing we noticed was that the gallon-per-minute (GPM) flow rate went from 1.3 to 2.0 GPM, so we instantly knew we had made an improvement before even doing the calculation for Reynolds number. This also changed the kinematic viscosity of the coolant from 5.25 KV with the 50/50 water to ethylene glycol mix to 1.31 KV with just water. We ran the calculation for Reynolds number again and it went from below 3,100 RN with water and 50/50 ethylene glycol mix to over 19,000 RN with straight water, which means we now had turbulent flow.

Chart showing kinematic viscosity of fluid used in coolant system
Figure 2. Use this chart to find the kinematic viscosity of the fluid you are using in your coolant system.

Once we determined we had turbulent flow using just water for coolant, we started up the machine to run parts. Once the machine was up and running, we verified that the only change we made to the process was changing out the 50/50 water to ethylene glycol mix to just water. We allowed the machine to run for a period of time so that everything would reach thermal equilibrium. We collected parts and used the same procedure to collect part-temperature data. We found that the temperature on part A went from 195° to 185°F and part B went from 285° to 277°F. Although this was not a drastic change in part temperature, it was data showing that turbulent flow has better cooling than laminar flow.

Switching from a chiller to thermolator to raise mold temperature

On the next test, we switched over from a portable chiller to a thermolator so we could raise the mold temperature. Once we had the thermolator in place, we adjusted the setpoint to 70°F and started the machine up to run further parts for testing. Once again, we verified the only changes were the water temperature and changing from a chiller to thermolator. We allowed the machine to run for more than 45 minutes to help

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