WoodNotOil said:
Master of Sparks - I fully respect and agree with you that primary/secondary is the better way to go if you are starting from scratch. However, some of us have to start with what we have.
When a zone calls for heat P2 does not automatically run. There would need to be an aquastat, probably on the exit pipe of the oil boiler, that tells P2 to run when the oil boiler needs heat. The differential should not be too low on zone return temps to prevent the water circulating from the tank to heat the oil boiler.
The tank to oil boiler piping in my diagram is just a copy of the tarm to oil boiler conection. On my system this works fine even with a 007 circ moving the water between boilers. This even works if all zones are calling for heat, which has happened. So I would assume this should work
"You comment about “steals some heat from the tank” is my quandry."
All I mean by this is that the flow will be split between the zone(s) calling for heat and the flow to charge the tank. This water will be up to temp because it is coming from the tarm.
I agree that a straight forward piping that can be measured and predicted is ideal. However, I think storage, both pressurized and non-pressurized, can be successfully implimented with series/parallel systems.
I think, without P2 running, with a zone calling for heat, the blue line is the flow path. So there is no "incentive" for flow from the buffer. Maybe the aquastat should measure the buffer temperature, not the boiler outlet? that way you would use the buffer to the lowest possible temperature. but again the tankless coil in the oil boiler for DHW limits how low you could draw down the buffer temperature.
A thought on efficiencies. I think there are a number of different efficiencies at work in these systems.
Combustion efficiency, how well the boiler turns the chemical energy stored in the cord wood to thermal energy. This is what draws me to gasification units. Currently that looks to be the best technology to get mid 80%. A combustion analyzer might be the tool to check that.
Then the boiler HX efficiency. How well does the design of the boiler transfer the energy from the fire to the water jacket. Stack temperature, a BTU meter could help determine that.
Then the piping or transmission efficiency. Pipe size, circ size, insulated piping and components, etc. The pipe should be sized to handle the flow with a 3.2 to 4 fps flow at the required gpm rate.
The circ should be sized to move that load with the least amount of electrical consumption. Keeping high pressure drop components out of the system helps, like 3 way thermostatic valves.
Distribution efficiency to the space. An example might be the use of transfer plates in radiant applications instead of staple up tube. The ability to transfer all the energy from the water flow, through the tube wall to the floor and into the space. I'd include insulation in this category, either the foam used under slab radiant or the insulation used under staple up applications. assure the heat is going where you want it with the least amount of loss to the ground or room below.
The biggest, and easiest to "tweak" efficiency would be the building or structure. Limit the heat loss from the building as much as possible BEFORE you design the heating, or cooling system. You'd be surprised what a few tubes of caulk and some weatherstrip upgrades can do to building infiltration.
I like chasing all those numbers. It is a never ending challange as technology continues to improve. Spray foam insulation, gasification boilers, mod con boilers, weather responsive controls, ECM circ pumps, etc. these are all products that have come along since I built my last home.
That is what keeps this business so fun and interesting for me. The next 10 years may be the golden years with fuel prices going crazy. i've seen figures on how much electrical energy could be saved if every refrigerator used ECM motors. consider millions of coke machines and refrigerated cases in grocery markets, etc.
Any ways, back to my solar project in the shop.
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