Single phase VSDs can be had fairly cheaply and are also a viable alternative to a motor starter. My experience with them is limited but controlling speed remotely shouldn't be hard if you've got a graphical PLC frontend. In fact if you have the right control program you could even control it using feedback from a temp probe i.e. it will throttle flow to achieve a target temp through a chiller. With minimal head in a system like this a centrifugal pump will control well.
Single phase VSDs aren't common but they are available, one example here: http://www.invertekdrives.com/variable-speed-drives/optidrive-e2-single-phase/
20mins for cast out is pretty standard timing, it allows the use of smaller HX and pumps. No point in thrashing things when you don't need to.
In your shoes I'd be looking to put some form of trub trap in the whirlpool rather than a filter in the cast out line. Commercial scale breweries don't need to, whirpool efficiency scales with diameter.
What I do for hoppy beers is use an immersion chiller to knock the temp down to 70C in 5 minutes time. That gets the temp below isomerisation AND volatilisation temps for most hop oils. Might be worth thinking about such a thing. Might not be worth spending on it.
Also, in addition to what LC said, you're not going to get a crapload more isomerisation after a 60-90 minute boil. It's not a straight-line process. The majority of the isomerisation will have occurred at that point. Enough so that the additional amount could be estimated to an acceptable degree.
What's a manway cost? I know you're looking to do a slick commercial style system, but could you just use a chain hoist , davit arm, or other method to lift the MLT and tip it for quick emptying? I'm thinking of doing this in my own home 3v system so I can just dump it out hot and clean it straight away. MLT cleaning at the end of a brew day is my most hated chore.
Mash Tun
Just as a comparison very tall, your probably looking at 750mm wide tun. How wide did you go on the kettle/whirlpool or what height width ratio did you go with.
Oh... ok.Ignore this
Yeah at homebrew scale I haven't really seen any that are appropriate - but you are 100% correct. It also provides better pump stability. Given Husky already has the PLC that's great, but I think even a small 3/4" control valve will be at least $1000-1500. Of course homebrewers are resourceful, so I'm sure there are cheaper versions out there.Sounds like a complete pain in the arse Adr_0, it irks me to say but I reckon a control valve with a 4-20mA positioner on the discharge would be the simplest method to control flow with a unit of this scale. I haven't dealt with them in the food industry but in mining and paper they haven't proven to be cheap (Keystone, Pentair, Tyco, Fischer, Eaton and Metso [shudder] come to mind). Though nor is a VSD and any associated control hardware.
If you can do a jacket, that would be the way to go. You'd have to have a look at the fluid dynamics inside the jacket. I'm assuming the dimpled jackets are to develop and increase turbulence inside the jacket, but I haven't looked into that.Maybe just easier to add a bit of chilled water jacket to the kettle to knock to 70 pretty quick. Lately 80% of my hops have been going into the WP then chilling to 80 in 3-5 mins and I like what I'm getting so ideally replicate that but bigger.
Sounds like a complete pain in the arse Adr_0, it irks me to say but I reckon a control valve with a 4-20mA positioner on the discharge would be the simplest method to control flow with a unit of this scale. I haven't dealt with them in the food industry but in mining and paper they haven't proven to be cheap (Keystone, Pentair, Tyco, Fischer, Eaton and Metso [shudder] come to mind). Though nor is a VSD and any associated control hardware.
Oh... ok.
Curious what your thoughts were on trub removal - I think the 30mm high rings would be good and should hopefully not disturb the whirlpool too much, but they will a little. Perforated mesh could even be used, then a final solid sheet weir if the bottom is sloped would be great - but I think a gentle draw-off would still be required.
Y-strainers often come with a tap/threaded fitting for draining inside the mesh screen. You could have a fairly big one on the suction with a drain to a collection pot, and a smaller one on the discharge with a similar drain. It's not a good idea to pull flow away from the suction but you might be able to do it over a couple of runs. The discharge - to protect the plate HX - should be fine to drain. Note that y-strainers need to be mounted horizontally as well.
For Husky and ADR_0:
I can't help with trub traps: I've never worked in a brewery small enough for this to be an option, the one I made for home use turned out to be useless. I'm going to give a "Trub Trapper" a go on the next build.
what about some kind of rotating racking arm, set it for a high pick up and as the wort drops you'll be able to see where the best pozzy is and rotate as you see fit.
If you can do a jacket, that would be the way to go. You'd have to have a look at the fluid dynamics inside the jacket. I'm assuming the dimpled jackets are to develop and increase turbulence inside the jacket, but I haven't looked into that.
Which pumps did you go with?Pumps ordered - Decided to order three pumps to allow the mash tun to recirculate while the kettle whirlpools if ever doing a back to back brew day to save time.
Which pumps did you go with?
Also, have a look at the Duda Diesel exchangers. They have some good larger ones, and have a great reputation. Although, that's a great price on the one you posted.
That was the point of no return!! Wow
Enter your email address to join: