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Who are we talking about customer or engineers (or both) LOLYes I do think that
but I as well as you know they don't do this most don't even know how to programme a digital time clock or a stat
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Discuss Calculate size of low Loss Header in the Plumbing Jobs | The Job-board area at Plumbers Forums
Who are we talking about customer or engineers (or both) LOLYes I do think that
but I as well as you know they don't do this most don't even know how to programme a digital time clock or a stat
Who are we talking about customer or engineers (or both) LOL
Me and Chris Watkins had a look at it last night briefly and actually couldn't quite work out the example above. If I get a chance I will try and get confirmation from the source.
If got a spread sheet somewhere for sizing LLH's i'll see if I can dig it out. Never used it myself, but was given to me by a heating consultant who teaches on HETAS courses so must be reasonably accurate, i hope!
PerfectIf you guys were stood in front of the boiler and knew what was being connected to the boiler from the system, all the different circuits and the boiler needed to be 50kW as a rule of thumb, what length and diameter LLH would you suggest this chap fits, you must have some idea and as Tamz says it would not hurt to be even a few diameter oversized, " would it", shall I have a stab, 100 mm dia MS 750 mm long, am I anywhere near, have to be welded up and would not look good in a kitchen, just a thought rule of thumb.
I shall I have a stab, 100 mm dia MS 750 mm long, am I anywhere near, have to be welded up and would not look good in a kitchen, just a thought rule of thumb.
If you have the Domestic Heating Design Guide it is section 13.8 (well it is in my old one)
flow rate = H / (TD x SH) = kg/s where
H = heat output in watts (50kW = 50,000 watts)
TD = temperature difference between flow & return in deg C (either 11 old or 20 new systems/boilers)
SH = specific heat of water in J/kg (which is 4186)
So flow rate = 50000 / (20 x 4186) = 50000 / 83720 = 0.5972 kg/s round it up to 0.6 kg/s
Using Tables 13.1a & b look down the column's of figures until you see >0.6 above the 0.5 m/s Velocity line that works it way across the table/page, in this case it appears in the first column on table 13.1b which is 42mm pipe size but it is only just, it might be better to use the next size up i.e 54mm in which case the velocity would drop to around 0.3 m/s.
So rule of thumb boilers up to 50kW can be connected to a 54mm copper L.L.header if using a delta T of 20deg C.
The pipe work connections should be arranged so that all the flows are at one end & all the return are at the other with a reasonable section of clear pipe between (say 150mm or 5 x inlet pipe dia minimum)
The F&R to boiler/s could be sized in the same way as about but normal velocity for domestic systems is <1.0 m/s or use the quick pipe sizer 13.2 (28mm can carry upto 40,000 to little & 35mm upto 62,000) so 35mm it is.
Better to arrange header so it is in the vertical (air & dirt separation) & make sure it has an AAV on top end & drain off on bottom.
Anyone got any thing to add (have I got it right ?)
Tamz,
Was that a good guess Tamz, your formula was near enough.
Doesn't mean it or I am right does it, looking for your input. Which might be useful to us all.You tell us you're the instructor, sounded impressive
Your just the bl**dy same as the rest of my students, attention span of a goldfish. LOLGoing so well and then i got bored towards the end lol!
Your just the bl**dy same as the rest of my students, attention span of a goldfish. LOL
Bit of 100mm box section plate top and bottom any one ?