LizardRuss
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- Aug 8, 2013
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I'm planning to build a brew stand and re-purpose my all-copper CFC as a HEX, similar to what is described here. I'll be recirculating both the HTL and MLT, both with tangential return ports. This will hopefully remove the need for stirring.
I will also monitor the temperatures through a dial thermometer installed on the HLT, and then a thermometer at both the input and output of the MLT. The MLT is a rubbermaid drinking cooler, so I'm curious to see how much of a temperature difference there will be between the two.
I have a couple questions for those with experienced with this type of set up.
My initial goal is only to keep the temperature stable. With my current set up, I don't have a way to monitor mash temperature, so I've only been making guesses. For example.. start the mash at 154, and finish the mash at 148... the target temperature being 151. I'll consider the new system a success if I can keep the mash temperature either steady, or at least above 150.
I don't have much hope for being able to do a step mash with my planned control method, since I'm essentially heating all of the water used in the brewing process with greater heat losses. I imagine I will just have to try it and see, unless someone's already tried this and can save me some time
Another downside to my control method is that the HLT will not be up to sparge temperature at the end of the mash. I may try a mash out, but it could take too much time to be practical. Worst case I can stop recirculating the HLT and heat it up to sparge temps.
I will also monitor the temperatures through a dial thermometer installed on the HLT, and then a thermometer at both the input and output of the MLT. The MLT is a rubbermaid drinking cooler, so I'm curious to see how much of a temperature difference there will be between the two.
I have a couple questions for those with experienced with this type of set up.
- Does using a tangential return in the MLT still require stirring in practice? I can see where the grain bed would prevent a lot of circulation and lead to stratification. I have the MLT set up so I can still remove the lid during the mash to stir if required.
- Is it possible to control this by hand? Automation isn't in the budget for a while. My planned strategy for manual control is to have a constant recirculation rate for both the HLT and MLT, and control the temperature using the HLT burner. In theory this would make the system an (in)direct fired mash, albeit with higher temperature losses, and I'd effectively be heating double the volume of water.
- From the graphs posted here it looks like the control method is maintaining the HLT temperature and cycling its pump on and off. Is this the only practical way to achieve a step mash with this system, or is it just the way its been implemented?
My initial goal is only to keep the temperature stable. With my current set up, I don't have a way to monitor mash temperature, so I've only been making guesses. For example.. start the mash at 154, and finish the mash at 148... the target temperature being 151. I'll consider the new system a success if I can keep the mash temperature either steady, or at least above 150.
I don't have much hope for being able to do a step mash with my planned control method, since I'm essentially heating all of the water used in the brewing process with greater heat losses. I imagine I will just have to try it and see, unless someone's already tried this and can save me some time
Another downside to my control method is that the HLT will not be up to sparge temperature at the end of the mash. I may try a mash out, but it could take too much time to be practical. Worst case I can stop recirculating the HLT and heat it up to sparge temps.