1
12
2
C
CH
HE
EC
CK
KIIN
NG
G IIN
NP
PU
UT
T R
RA
AT
TE
E
T
Ta
ab
blle
e 4
4 -- M
Me
ette
err--T
Tiim
miin
ng
g G
Ga
as
s
Time required for one revolution is charted for various size
meter dials and various rates of gas input in cu. ft. per hour. To
convert to BTUH, multiply by the heating value of the gas
used.
T
Tiim
me
e ffo
orr 1
1
IIn
np
pu
utt,, C
Cu
u.. F
Ftt.. p
pe
err H
Ho
ou
urr,,
R
Re
ev
vo
ollu
uttiio
on
n,,
W
Wh
he
en
n M
Me
ette
err D
Diia
all S
Siiz
ze
e iis
s::
1
1//2
2 c
cu
u.. fftt..
1
1 c
cu
u.. fftt..
2
2 c
cu
u.. fftt..
5
5 c
cu
u.. fftt..
10
180
360
720
1800
12
150
300
600
1500
14
129
257
514
1286
16
112
225
450
1125
18
100
200
400
1000
20
90
180
360
900
22
82
164
327
818
24
75
150
300
750
26
69
138
277
692
28
64
129
257
643
30
60
120
240
600
35
51
103
206
514
40
45
90
180
450
45
40
80
160
400
50
36
72
144
360
55
33
65
131
327
60
30
60
120
300
70
26
51
103
257
80
22
45
90
225
90
20
40
80
200
100
18
36
72
180
120
15
30
60
150
S
Se
ec
c..
T
Ta
ab
blle
e 6
6 -- O
Orriiffiic
ce
e D
Drriillll S
Siiz
ze
es
s w
wiitth
h D
De
ec
ciim
ma
all E
Eq
qu
uiiv
va
alle
en
ntts
s
M
Ma
aiin
n B
Bu
urrn
ne
err O
Orriiffiic
ce
es
s
D
Drriillll
D
Diia
a..
D
Drriillll
D
Diia
a..
S
Siiz
ze
e
D
De
ec
ciim
ma
all
S
Siiz
ze
e
D
De
ec
ciim
ma
all
E
Eq
qu
uiiv
va
alle
en
ntt
E
Eq
qu
uiiv
va
alle
en
ntt
48
.0760
31
.1200
45
.0820
30
.1285
43
.0890
27
.1440
42
.0935
26
.1470
40
.0980
25
.1495
37
.1040
23
.1540
20
.1285
P
Piillo
ott O
Orriiffiic
ce
e S
Siiz
ze
es
s ((iin
nc
ch
he
es
s))
P
Piillo
ott T
Ty
yp
pe
e
N
Na
attu
urra
all
P
Prro
op
pa
an
ne
e
J640DHA
.015
.010
J993DHW
0.18
.010
J994DHW
Q345
.018
.012
5CHL-6
.018
.010
5SL-6ER
.018
.010
T
Ta
ab
blle
e 5
5 -- M
Ma
an
niiffo
olld
d P
Prre
es
ss
su
urre
e a
an
nd
d G
Ga
as
s C
Co
on
ns
su
um
mp
pttiio
on
n**
T
Ty
yp
pe
e o
off G
Ga
as
s
N
Na
attu
urra
all
P
Prro
op
pa
an
ne
e
M
Mo
od
de
ell
B
BT
TU
U//C
Cu
u.. F
Ftt..
1
10
04
40
0
2
25
50
00
0
N
No
o.. o
off
S
Siiz
ze
e
S
Sp
pe
ec
ciiffiic
c G
Grra
av
viitty
y
0
0..6
60
0
1
1..5
53
3
O
Orriiffiic
ce
es
s
M
Ma
an
niiffo
olld
d P
Prre
es
ss
s.. IIn
n.. o
off H
H2
2O
O
3
3..5
5
1
10
0""
Cfh
72.1
30.0
D
DJ
JE
E7
75
5
✝
Gal./Hr. Propane
–
.82
1
SEC/Cu. Ft.
50
120
Orifice Drill Size
20
37
Cfh
96.1
40.0
D
DJ
JE
E1
10
00
0
✝
Gal./Hr. Propane
–
1.09
2
SEC/Cu. Ft.
37.5
90
Orifice Drill Size
30
45
Cfh
120.2
50.0
D
DJ
JE
E1
12
25
5
✝
Gal./Hr. Propane
–
1.37
3
SEC/Cu. Ft.
29.9
72
Orifice Drill Size
31
48
Cfh
144.2
60.0
D
DJ
JE
E1
15
50
0
✝
Gal./Hr. Propane
–
1.64
3
SEC/Cu. Ft.
24.9
60.0
Orifice Drill Size
30
45
Cfh
192.0
80.0
D
DJ
JE
E2
20
00
0
✝
Gal./Hr. Propane
–
2.19
3
SEC/Cu. Ft.
19
45
Orifice Drill Size
23
40
Cfh
216.3
90.0
D
DJ
JE
E2
22
25
5
✝
Gal./Hr. Propane
–
2.46
3
SEC/Cu. Ft.
16.6
40.0
Orifice Drill Size
20
37
Cfh
240.0
90.0
D
DJ
JE
E2
25
50
0
✝
Gal./Hr. Propane
–
2.74
4
SEC/Cu. Ft.
15
36
Orifice Drill Size
25
42
Cfh
288.4
120.0
D
DJ
JE
E3
30
00
0
✝
Gal./Hr. Propane
–
3.28
5
SEC/Cu. Ft.
12.5
30.0
Orifice Drill Size
26
43
Cfh
336.0
140.0
D
DJ
JE
E3
35
50
0
✝
Gal./Hr. Propane
–
3.83
6
SEC/Cu. Ft.
10.7
25.7
Orifice Drill Size
27
43
Cfh
385.0
160.0
D
DJ
JE
E4
40
00
0
✝
Gal./Hr. Propane
–
4.37
6
SEC/Cu. Ft.
9.3
22.5
Orifice Drill Size
23
40
*Above gases based on average standards. Units can be furnished for gases of
different values and specific gravities. (
✝
Gal./Hr. based on 60°F. 30" Hg., 91,500
BTU/Gal.).
In Canada, refer to rating plate on side of unit for orifices at high altitude.
Summary of Contents for DJE
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