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MG Thermal Consulting

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Posts posted by MG Thermal Consulting

  1. Jay, matching up the chiller to the reservoir is the key, but also the jacket performance! I am waiting on a couple fellows who are testing their jackets (with city water, figuring out the flow and measuring the Temp in and out with a simulated test run using water. This way I can match all three exchange devices and quote the proper system. Cheapest way on the reservoirs is to gang together several poly tanks (square ones work best for cutting holes and attaching fittings). If you can find a used bulk milk tank to store the water, that may even be cheaper. Right now all I have as far as used chillers go is a 9 ton 460/3/60 and a 2 ton 230/1/60. Let me know if I can be of any further help. Mike

  2. If you are using a "closed loop", if you trim (control flow) to a load, you need to bypass the remainder available back to the main return line. As far as flow meters go, they are pricey and usually are used to secure a fixed flow rate. Flow regulators (either electronic or pressure actuated) come in two or three way varieties, the two way being less expensive, but you still need to add the bypass line, like you automatically have for the three way valve. With small diameter valves, the three way is a space saver as well. If you are running with city water, you obviously will have a wider swing, summer to winter- closed loop you can reset your reservoir tank or chiller op stat to a higher tempp if it is too cold for ya.

  3. Depending on the motor characteristics, how the pump is run on the pump curve can cause an overloading state (say deadheading a pump) that can cause the overloads to trip. Multiple occurrences of overload trips can in turn cause either failure of the overloads or the motor windings from the heat buildup.

  4. Depends on what the unfiltered "stuff" is, I guess.

    You take the "stuff" in cloudy wine and that is tartaric acid crystals, the sediment that can make some people sick.

    I have sold glycol chillers for cold filtering, so it is not uncommon. The glycol is supplied at around 25F, so it is usually a stand-alone chiller for that part of the process, and of course, another expense.

  5. And if you put a jacket on the tank, at least have it rated for 35 psig.

    You have a problem with cooling water flow (closed loop) when you try to set up a cooling system when the tank jacket is only good for 15 psi (used for steam heat on the front end).

    You wind up putting some expensive valves to ensure pressure from pump not bursting the jacket and still getting flow you need for cooling, especially if you have to get a modulating 3- way bypass valve, a bypass line, check valve and control for the 3 way valve. This can be an issue on mash tanks when you are told you can crash cool by pumping chilled water through the jacket after heating.

    Everyone should be well advised to find out what the capacity of the jacket (by experimenting if necessary) is for the jacket when pumping chilled water through it.

  6. If it has electrical components, UL has some interest. Other items having to do with safety as well.

    It also is used to standardize components (to be UL you have to use UL components).

    There are other testing agencies out there (ETL is another), but if you have UL components and the inspector doesn't budge, you will need to get it rated "in the field"...aka money to get a sticker.

    If you don't have components that are rated by some testing agency, it could get sticky.

  7. Sorry ...Yes, it is 208-230/1/60.

    It doesn't include a small water reservoir like most of these small chillers do because it was being used for an external reservoir (if you're going to use it for mash cooling, I suggest you get one about 2.5 times the volume of your mash tank- this keeps you from overheating the chiller when you being mash cooling). If you are just using it for fermenting control, you only need a small tank to act as reservoir to feed the pump or plumb it as a completely closed system with p/t valve, vent and expansion tank.

    Regards,

    Mike

  8. It is an understatement saying cost of electricity MAY not be as cheap in other parts of the country (world).

    Not only the cost of the electricity is important, but whether the distillery can physically install enough amperage and voltage.

    The last part cuts off many distillers right at the knees before they get started.

  9. I was curious about your study on relative operational costs of steam (gas fired) vs electric.

    Steam, while weighted heavy on first cost, is more efficient energy wise, no?

    If small set-ups are more efficient with electric, what is the top over point where steam is more efficient.

    I would assume also, some outfits would be located where enough electric power may not be available, all those in "agricultural zoned" permits, more than likely.

  10. Lb,

    I distribute a line of shell and tube mash exchangers, two week lead time from receipt of order and payment.

    I can sent a photo over to you if you email me at mikegronski@gmail.com

    I offer the closed loop system: chiller with chilled water pump, water reservoir and mash exchanger.

    Regards,

    Mike

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