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Boiler piping

Greg Maxwell
Greg Maxwell Member Posts: 212
I'm involved in a job where we are going to take 2- 7 section Biasi SG boilers and pipe them together to a common main. The boilers will be 1-1/2, piped into a 2" main. I would like to know if anyone out there has a piping diagram for injection from each boiler into the main, so I dont have to flow through both boilers at the same time. The boilers are going to be staged - lead/lag.

Comments

  • NYplumber
    NYplumber Member Posts: 503
    P/S

    Using primary/secondary you can join them in parallel into the main. I usually set the controls to alternate which boiler leads every X amount of hours.
    :NYplumber:
  • lchmb
    lchmb Member Posts: 2,997
    taco

    Has a nice control package for just this type of setup. Simple but effective...
  • Greg Maxwell
    Greg Maxwell Member Posts: 212
    Boiler piping

    We are going to be using an AQ251 H/W control on this, I am just wondering about piping the boilers into the main. I'd like to use injection. Each boiler will have its own pump.
  • Larry (from OSHA)
    Larry (from OSHA) Member Posts: 723
    edited August 2011
    you might try this

    The Knight install manual has great diagrams.   Page 40 might be what you are looking for.



    http://www.lochinvar.com/_linefiles/KBII-I-O%20Rev%20D.pdf





    Hope this helps.



    Larry
  • Jason_13
    Jason_13 Member Posts: 304
    Piping

    http://www.comfort-calc.net/Multiple_boiler.html

    Check this drawing one. It is very simple but the point is made.
  • CMadatMe
    CMadatMe Member Posts: 3,086
    Low Loss Header

    Gets piped the same way as multiple condensing boilers.



    http://www.caleffi.us/en_US/caleffi/Details/Magazines/pdf/idronics_1_us.pdf

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  • meplumber
    meplumber Member Posts: 678
    2" sounds small

    For 2- 7 section boilers.  My gut reaction would have been 3" or at least 2 1/2".
  • CMadatMe
    CMadatMe Member Posts: 3,086
    Pipe sizing

    ME is spot on. Each of those boilers has a heating capacity of 279. Boiler supply and returns need to be 2" and the header 3" to move the 558 if your designing around a 20 degree delta-t.

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  • Greg Maxwell
    Greg Maxwell Member Posts: 212
    Main Size

    Looking at a velocity of 5ft per sec for 50gpm, and a head of 4.6ft, my chart says 2".
  • hot_rod
    hot_rod Member Posts: 22,814
    parallel pipe

    them. It can be done with or without a hydro-separator, depending on your pumping requirements on the boiler and load side.



    Be sure the piping is sized for the flow rate you are desiging around.



    hr
    Bob "hot rod" Rohr
    trainer for Caleffi NA
    Living the hydronic dream
  • Greg Maxwell
    Greg Maxwell Member Posts: 212
    Parallel

    Rod, I like that piping diagram. I'll forward that onto the contractor. I however wont use a hydroseperator, I'll figure closely spaced tees. Seperators are an aweful lot of money for whet they are.

    Thanks
  • Jean-David Beyer
    Jean-David Beyer Member Posts: 2,666
    Seperators are an aweful lot of money for whet they are.

    Since I am not a pro, I do not know the answer to this question. I know what the manufacturers of hydraulic separators say.



    If you include the cost of an air extractor and a dirt separator, and the labor of plumbing them in, is the cost of an separator still unreasonably high?
  • CMadatMe
    CMadatMe Member Posts: 3,086
    Exactly

    And we haven't even talked about no temp drops across the zones.

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  • Jean-David Beyer
    Jean-David Beyer Member Posts: 2,666
    no temp drops across the zones

    Can you explain that? If you have closely-spaced Ts instead of hydraulic separator, and the common pipe on the load side is sufficiently large (which would be required with hydraulic separator as well), you would not get temperature drops with the Ts either, it seems to me. Drops with Ts would be a problem if you used separate pairs of Ts in series, one for each load (which would make sense sometimes).
  • Greg Maxwell
    Greg Maxwell Member Posts: 212
    Hydraulic seperators

    Yes, by hundreds
  • CMadatMe
    CMadatMe Member Posts: 3,086
    Not On a 20

    Degree delta-t you won't. Need 2-1/2 at 5ft per second. Ran it thru Siggy's software just to check myself.

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  • CMadatMe
    CMadatMe Member Posts: 3,086
    No Temp Drops

    Because I would be piping antler style as shown in HR's pic above on the secondary side. You might be interested in these JD



    http://www.caleffi.us/caleffi/en_US/Site/Technical_library/Idraulica_magazine/index.sdo

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  • NYplumber
    NYplumber Member Posts: 503
    Buffer

    Buffer tanks offer a lot in one package. I have been incorporating them into all my installations and have been more than pleased with the outcome. Results are as follows: air separation, dirt separation, hydraulic separation, parking space for btus, and if there is an internal coil, hot water or snow melt can be used too.



    :NYplumber:
  • meplumber
    meplumber Member Posts: 678
    2" Pipe.

    The last time I looked, 2" pipe would only carry about 450 MBTU at a 20* delta T.  You need to up size to 2 1/2" to carry that load.  You calculations didn't take into account the delta T.
  • Jean-David Beyer
    Jean-David Beyer Member Posts: 2,666
    I have looked at Caleffi's hydraulic separators...

    ... and they seem to be fine devices. If you do not get labor for free, it seems to me that it makes a lot of sense to use one of these instead of closely spaced Ts, an air extractor, and a dirt separator.



    However, the losses to which you allude would be the same whether you used closely spaced Ts near the boiler supply and return, or whether you used an hydraulic separator. On the load side, if plumbed as in the illustration, above, the parallel piping would be the same whether one used an hydraulic separator or the closely spaced Ts. The thing called "field constructed headers (typical)" would determine the temperature loss between the various load circuits, and provided those are of sufficient diameter, the loss should be negligeable.
  • CMadatMe
    CMadatMe Member Posts: 3,086
    Pri/Sec

    Your correct in that blending inside the LLH produces as drop in water temp but I am referring to a drop across the zones as multiple zones open. In a true primary secondary piping arrangement you do. I'm using my i-pad so don't have a diagram to show you but did find this nice articlen written by our host.





    http://t4engr.com/understanding_primarysecondary.htm

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  • CMadatMe
    CMadatMe Member Posts: 3,086
    Wrong thread

    Hey ME that was his other thread on the piping. I think you mean 35gpm on a 20.

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  • Jean-David Beyer
    Jean-David Beyer Member Posts: 2,666
    I am referring to a drop across the zones as multiple zones open.

    I do not know what you mean by a "true" primary-secondary piping arrangement. There are several primary-secondary arrangements I have seen. One is shown in the diagram that appears earlier in this thread. I would consider that "true". Another would have a series loop on the load side of the closely spaced Ts, with a set of closely spaced Ts for each load drop; there would be a circulator to drive flow through this secondary loop. I would consider this as "true" as the first.  In this arrangement, the first load loop, would get the hottest water, and each following loop would get colder water (assuming all loops were running). But this would be the same whether the primary loop (the one containing the boiler(s)) were separated from the secondary loop by closely spaced Ts or an hydraulic separator.
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