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application of cbm gas on rotary kiln

kiln gas in contact with the wall be estimated from hgw 0036 933rD 055 2 where kg is the thermal conductivity of the gas D is the kiln ID and L is the kiln length This equation is for turbulent flow For the low gas flow rates examined here hgw 2 W m2 K This would obviously be higher if the flame impinged on the bed

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