[0, ki] 1^m-Factorizations Orthogonal to a Subgraph by Ma R., Xu J., Gao H.

By Ma R., Xu J., Gao H.

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16 . 18 20 22 ~~ ~ 24 26 28 30 32 34 HEAT LOSS AS PER CENT OF CALORIFIC VALUE HEAT LOSS IN FLUE GASES FOR TOWN GAS 36 38 Combustion 35 S e n s i b l e h e a t c a r r i e d a w a y by flue g a s e s i :y 14 _ ~ N. 12 ~ 10 . . 9 \ \ ~ . 5 ! , ~.. 8 - 7 L k~- \'~'~-k \ ~ 6 10 12 14 16 18 20 22 24 26 28 HEAT LOSS AS PER CENT OF CALORIFIC VALUE HEAT LOSS IN FLUE GAS FOR GAS OIL 30 36 HVAC E n g i n e e r ' s H a n d b o o k Chimney sizes Theoretical c h i m n e y d r a u g h t where h - d r a u g h t in m m w a t e r height in m T 1 - absolute t e m p e r a t u r e outside c h i m n e y K T 2 - absolute t e m p e r a t u r e inside c h i m n e y K H-chimney where h = draught H-chimney T1--absolute T 2 - absolute in inches of w a t e r height in ft t e m p e r a t u r e outside c h i m n e y ~ t e m p e r a t u r e inside c h i m n e y ~ Chimney area The chimney should be designed to give a m a x i m u m velocity of 2 m / s (7 f t / s ) for small furnaces, and 1 0 - 1 5 m / s for large furnaces.

The above formulae are for laminar flow. Flow is l a m i n a r if Reynolds N u m b e r (Re) is less t h a n 1500. Reynolds n u m b e r can be checked from the following formulae. As Re is a dimensionless ratio it is the same in all consist e n t systems of units. The coefficients in the following formulae take into account the dimensions of fl, dl, f2, d2 respectively. The viscosity to be taken is t h a t at the t e m p e r a t u r e of the oil in the pipe. Viscosity at temp. l r'l II: 0 l. I I L------------------- --- ?

001 I I~"~ 6 kt wsr 2 The Increased Heat Requirement of Buildings during the heating up period causes a greater heat requirement than the steady state. This additional heat loss depends mainly on the type of building, length of heating interruption and heating up time, and type of heating installation. The allowance for covering the increased heat loss during heating up is usually expressed as a percentage of the heat loss in the steady state. See pages 91 and 92. The temperatures during warming up of bodies are represented graphically by curves which are symmetrical to cooling down curves.

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