I figured I already have a nice heat exchanger to chill so why not use it to heat as well.
because of properties that no one usually thinks about...
what makes a good herms coil doesnt make a good chiller, and vice versa. the operational requirements for each are much different. for the chiller, you want maximum possible surface area of the heat exchanger to make more efficient use of each gallon of chilled water. the ability to quickly cool the wort is only secondary to that because it can be made up for by simply wasting lots of water.
for a HERMS coil, the goal is mainly to keep a very tight temperature tollerance, and also it needs enough flow as to not bog down the pump and so that the temperature change is reflected quickly in the mash itself. low flow can be made up for by increasing the legnth of the coil ind increasing the HERMS exit temperature, but at the expense of not being able to drive the heater as hard, or at the risk of overshooting your temperature in the mash itself. the longer the wort sits inside the coil, the more it will heat. if its spending a long time in the coil, the temperature difference between the wort and water bath cant be as large (and thus, heat flux will be lower, and wort heating will be less efficient). also- the more poorly your HERMS is designed, the more you will need to rely on good PID settings to make up for it.
so for a chiller; the ideal design would be one, or several parrallel, long thinner legnths of coiled copper tube. a HERMS coil would idealy be a short, thicker-ID coil. any dual-use designs would only be a compromise between the two optimal designs of each use. there are also
many... "non-ideal" lets call em, designs floating around the internet. people stick 100 feet of 3/8" copper in a 15gallon HLT and call it a HERMS. do these designs work? sure... it seems to make beer... so no one gives it any more thought.
you
can use one for the other, the same way you
can use a torx bit to drive an allen-keyed screw.
QUESTION: PID in HERMS set- up is controlling the mash temp via the temperature of the HLT. So the feed back for the PID is the mash temp, correct?
more accurately it should be the HERMS output temperature. if you are measuring only the mash temperature, and it takes 5-10 minutes for a temp change to be registered by that temperature probe, you could be denaturing all the enzymes that flow thru the HERMS coil for those 5-10 minutes. if your flow rate is .5gpm, and your total mash has 10 gallons in it, 30-50% of your enzymes could be denatured before the controller turns off the heat. also the "farther away" your probe is from the controlling heat source, the greater the error you will have.