5. Gas connection
45
EN
•
Measure the connected gas flow
pressure.
This must agree with the
details on the rating plate. If pressure is
too high, install a pressure regulator.
•
Attention: If the measured gas flow
pressure deviates from the values in
the table, the gas supplier must be
informed:
If the connected gas flow pressure is
outside the permitted range, the
appliance must not be operated. The gas
supply to the appliance will have to be
sealed.
•
Attention!
In order to ensure that the
appliance's factory setting is compatible
with the on-site connection conditions, an
exhaust gas analysis must be performed
after the first operation of the steam and
convection burners (CO, CO2). The
relevant values must be documented in
the unit.
•
CO
2
values:
Natural gas
8.6 – 9.6 %
Liquid Propane
10.0 – 11.0 %
Liquid Butane gas! 11.7 – 12.7 %
•
For values of
undiluted CO > 1000 ppm
the
burner setting
and the appliance
must be
checked
and, if necessary,
adjusted
by a
trained
service
specialist
. The appliance may only be
operated for maintenance and adjustment
purposes. Ensure adequate ventilation of
the workplace!
•
Heat output of the gas appliance in kW
Unit size
6.10
6.20
10.10
10.20
12.20
20.10
20.20
Convection burner
12
20
20
35
40
40
70
Steam generator burner
(only in OGB)
12
18
18
30
35
30
35
•
Gas data (according to CE standards) at 15°C and 1013 mbar dry
Family
Gas type and
Symbol
Wobbe index
inferior superior
Net calorific value Gross calorific value
Wi
Ws
Hi
Hi
Hs
Hs
Rated
connection
flow
pressure in
mbar
MJ/m3
MJ/m3
MJ/m3
MJ/kg
MJ/m3
MJ/kg
2H ( E ) Natural gas (H)
G20
17-25
45.7
50.7
34.0
--
37.8
--
2L ( LL ) Natural gas (L)
G25
18-30
37.4
41.5
29.3
--
32.5
--
3B
Liquid Butane
gas G30
25-57.5
80.6
87.3
116.1
45.7
125.8
49.5
3P
Liquid Propane
gas G31
25-57.5
70.7
76.8
88.0
46.4
95.7
50.4
•
Gas appliance gas consumption
Unit size
6.10
6.20
10.10
10.20
12.20
20.10
20.20
Natural gas (H) G20
m
3
/h
1.3
2.1
2.1
3.7
4.2
4.2
7.4
Natural gas (L) G25
m
3
/h
1.5
2.5
2.5
4.3
4.9
4.9
8.6
Liquid gas G30/G31
kg/h
0.9
1.5
1.5
2.7
3.1
3.1
5.4
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