Expansion Vessel; Pump Controlled Pressure Maintaining Systems - Viessmann Vitoplex 100 Service Instructions For Contractors

Oil/gas boiler
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Checking the expansion vessel and system...

Expansion vessel

1. Drain the system until the pressure gauge indi-
cates "0" or close the cap valve on the expansion
vessel and reduce the pressure in the expansion
vessel.
Note
The pre-charge pressure of the expansion vessel
(p
) is made up of the static system pressure (p
0
(= static head) and a supplement (p
plement).
The supplement depends on the high limit safety
cut-out setting. The following high limit safety cut-
out settings apply
100 °C: 0.2 bar (0.02 MPa)
110 °C: 0.7 bar (0.07 MPa).

Pump controlled pressure maintaining systems

!
Please note
Pressure fluctuations may cause damage to the
boiler or to other system components.
In heating systems with automatic pressure
maintaining systems, and in particular pump
controlled systems with integral deaeration, we
recommend the installation of a diaphragm
expansion vessel for individual boiler protection.
This reduces the frequency and level of pres-
sure fluctuations. This in turn contributes signifi-
cantly to improved operational reliability and a
longer service life of the system components.
Boiler out-
kW
put
Expansion
litres
vessel
Checking the temperature controller setting if a building management system
is used (DCC system)
!
Please note
Shutting down from full load can result in high
material stress and material damage to the
boiler.
If a system with a higher ranking building man-
agement system takes over the temperature
control of the boiler, adjust the settings at the
temperature controller TR. Set the electronic
temperature controller TR to at least 10 K below
the mechanical temperature controller TR of the
Vitotronic.
For water quality requirements, see page 20.
*1
St
= p
+ sup-
0
St
Up to
Up to
Up to
300
500
1000
50
80
140
Commissioning, inspection, maintenance
(cont.)
2. If the pre-charge pressure of the expansion vessel
is lower than the static system pressure, top up
with nitrogen until the pre-charge pressure is 0.1 to
0.2 bar (0.01 to 0.02 MPa) higher.
The static pressure corresponds to the static head.
3. Top up with softened water
)
sure of the cooled system is 0.1 to 0.2 bar (0.01 to
0.02 MPa) higher than the pre-charge pressure of
the expansion vessel.
Permiss. operating pressure: 5 bar (0.5 MPa)
!
Please note
The ingress of oxygen can result in system dam-
age as a consequence of oxygen corrosion.
Only use pump controlled pressure maintaining
systems that are sealed against corrosion. The
pressure maintaining systems must be protected
against oxygen ingress into the heating water.
Pump controlled pressure maintaining systems
with atmospheric deaeration through cyclical
pressure release bring about central post-venti-
lation of the heating system. They do not pro-
vide oxygen removal in the sense of corrosion
protection as described in guideline VDI 2035
part 2.
Carry out all checks in accordance with the manufac-
turer's instructions. Limit pressure fluctuations to the
lowest possible differential. Cyclical pressure fluctua-
tions and more significant pressure differentials point
towards a system fault. Immediately remedy such
faults, otherwise other heating system components
may suffer damage.
*1
until the charge pres-
11

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