DESIGN OF OPEN-HEARTH FURNACES
27-5
Gas on Gas
Air on Air
Gas on Waste Gas
Air on Waste Gas
Space required in chamber above checkerwork by Yesmann's formula, which was used in obtaining the height of the heating chamber For the case in hand: QQ — volume of gases per second 1° = temperature ............
5m3 32 1200°
8m3 51 1200°
5m3 19 1600°
7m3 58 1600°
1 -{-at = gas temperature factor .... Qi=Qo(H-«£) = ...
5.404 28 m3 75
5.404 45 m3 99
6.872 35 m3 66
6.872 52 m3 08
0,2= .............
827
2115
1272
2712
B — width of chamber =
3m 483
5 m 763
3 m 483
5 m 763
B2= .......................
12.13
33.21
12.13
33 21
BH=- ..........
14,543
39,852
19408
53 135
Q?-i-Bn= . ...........
0 05686
0 05306
0 06555
0 05104
<\/Qt* + BH = X= .............
A ~~ coefficient
0.3845 3 40
0.3758 3 53
0.4032 3 40
0.3710 3 53
ht = AX .
1 m 306
1 m 327
1 m 372
1 m 310
Rise of arch over chamber ......
0 m 420
0 m 700
Checker to skewback ...........
1 m LSO
0 m 900
Chamber above checkerwork: The frictional resistance to the flow of the gases will be about equivalent to the full volume for one-third the length m = coefficient of friction = . , . • S = perimeter = (2X3. 483) + (2X1 250)==
0.016
9 466
L — length .....
2 554
8 = perimeter = (2 X 5 . 763) + (2X1 250) =
14 026
w = area = 3. 483X1. 250=...
4 354
co = area = 5. 763X1. 250 = ...
7 203
SL+u= 9.466-^-4.354 = .......
2 174
£L-r-co = 14 026-T-7 203= .......
1 947
^ = Qjj -T- co = m per sec .......
6.60
6 39
8 19
7 23
AO — specific weight gas . . .
1 125
1 293
1 32
1 32
A;=A0-KH-<*0 kg per m3. . .
0.2082
0.2393
0.1921
0.1921