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Thanks Dear Brother for this video. But I don’t understand 5680 kg/hr ÷ 810 kg/hr =7 kg/hr steam only?? Please clear me.
Very good and simple explanation Sir Thanks!. can u please write boiler steam temperature?
Heat available should consider a T1 about 200 grades C to avoid condensation at the discharge ? Why you calculate on 30 degrees ? Isn’t it unreal that you would let that exhaust gases at 30 degrees ?
perfect videos perfect explanation thank youuu
Good
Keep struggling brother 🤨
Regarding T1, the exhaust flue gas temperature should be above the sulphur condensation(dew) point(at least about 160°C ), is it correct?
But generator load is not constant, how to calculate WHRB capacity at 70, 80 & 90% of generator load.....
This awesome and educational. Could you plz share your email so that we can relate
That is awesome. Thanks a lot sir.
thank you for this video sir
Sir,This video is very informative but mostly part of this video is not visible. Please share formula in soft form if possible. Thank you.
Thanks Dear Brother for this video. But I don’t understand 5680 kg/hr ÷ 810 kg/hr =7 kg/hr steam only?? Please clear me.
Very good and simple explanation Sir Thanks!. can u please write boiler steam temperature?
Heat available should consider a T1 about 200 grades C to avoid condensation at the discharge ? Why you calculate on 30 degrees ? Isn’t it unreal that you would let that exhaust gases at 30 degrees ?
perfect videos perfect explanation thank youuu
Good
Keep struggling brother 🤨
Regarding T1, the exhaust flue gas temperature should be above the sulphur condensation(dew) point(at least about 160°C ), is it correct?
But generator load is not constant, how to calculate WHRB capacity at 70, 80 & 90% of generator load.....
This awesome and educational. Could you plz share your email so that we can relate
That is awesome. Thanks a lot sir.
thank you for this video sir
Sir,
This video is very informative but mostly part of this video is not visible. Please share formula in soft form if possible. Thank you.