What does the building inspectors have to do with a floor heat upgrade? If you stay under 199k for each heater, you can do it yourself. No boiler liscence needed....Or will it need to be inspected regardless of who does the work? I don't have to deal with any of that where I'm located. Maybe you can contact the inspectors to see what is required, first step? BTW, 20 "Something" thousand seems rediculous! I did my single heater and pumps for under $2500. And the Takagi's are now cheaper than when I did my install...$1200 and some change each!Back to the drawing board on this as he said the install would be in the upper 20 something thousand. He is willing to install two tankless water heaters but needs someone else to design the system. He said the price would not exceed $9K depending on the units and pumps. Normally I would take on this project myself but we are going to have building inspectors in and out during this massive remodel.
I don't think "Cheating" the length to get heat to the area is what you need to be concerned with....It has to do with the size tubing you use creates its own head pressure depending on length. The longer the length, the more pressure you need to force the glycol through the lines. Larger lines require less pressure, smaller size pump/pumps...I'm sure you can find a head pressure calculator online to help give you the answers....You don't want to "Guess" at it!Also I need to design the tubing layout for two aprons. We are wanting to reuse the 1/2" 10 outlet manifold to keep it balanced with the self serve side. Is 190 feet the max run for 1/2"? Can we cheat the length a bit by insulating them until they get to the aprons? One apron is going to be about 65 feet from the manifold to the slab. That eats up 130 feet per run right there.
What does the building inspectors have to do with a floor heat upgrade? If you stay under 199k for each heater, you can do it yourself. No boiler liscence needed....Or will it need to be inspected regardless of who does the work? I don't have to deal with any of that where I'm located. Maybe you can contact the inspectors to see what is required, first step? BTW, 20 "Something" thousand seems rediculous! I did my single heater and pumps for under $2500. And the Takagi's are now cheaper than when I did my install...$1200 and some change each!
I don't think "Cheating" the length to get heat to the area is what you need to be concerned with....It has to do with the size tubing you use creates its own head pressure depending on length. The longer the length, the more pressure you need to force the glycol through the lines. Larger lines require less pressure, smaller size pump/pumps...I'm sure you can find a head pressure calculator online to help give you the answers....You don't want to "Guess" at it!
I’ve always used 200’ maximum length of loops – with a 10% variable. This eliminates the need for “balancing valves”
But, running all loops to and from the equipment room makes that design quite difficult.
Our solution is to install manifolds for every 2 bays…at the entrance or exit apron. We’ve even done manifolds on both sides of the bays; supply on one side, return on the other.
Our latest 6 bay installation features 4 manifold boxes. All piping from the equipment room is 1-1/2” PEX. The manifolds live in boxes set to finished floor height. With entry-side concrete heated to the building’s winter shadow line, these loops are approximately 165’ each (+ or - 16’).
View attachment 10042
And, another 3 loops per bay with ~165' loop installation in progress. The IR photo shows how effective the insulation is during "polar vortex" conditions. (-2 degrees).
View attachment 10044 View attachment 10045 View attachment 10046
Good measurements and planning are necessary to draw the map. I've spent many hours just refining layout drawings.
Also note the Ruud is listed as a combi boiler...You sure this is what you want? Heating mode looks to be only 120K BTU...
Sorry to be the "Debbie Downer"!That is odd and something I missed. Probably not going to work. There's always something.