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Carel EVD Evolution Twin - 10. TROUBLESHOOTING

Carel EVD Evolution Twin
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ENG
“EVD Evolution TWIN” +0300006EN - rel. 2.6 - 31.01.2019
55
10. TROUBLESHOOTING
The following table lists a series of possible malfunctions that may occur
when starting and operating the driver and the electronic valve. These cover
the most common problems and are provided with the aim of oering an
initial response for resolving the problem.
PROBLEM CAUSE SOLUTION
The superheat value measu-
red is incorrect
The probe does not measure correct values Check that the pressure and the temperature measured are correct and that the probe
position is correct. Check that the minimum and maximum pressure parameters for the
pressure transducer set on the driver correspond to the range of the pressure probe
installed. Check the correct probe electrical connections.
The type of refrigerant set is incorrect Check and correct the type of refrigerant parameter.
Liquid returns to the com-
pressor during control
The type of valve set is incorrect Check and correct the type of valve parameter.
The valve is connected incorrectly (rotates
in reverse) and is open
Check the movement of the valve by placing it in manual control and closing or ope-
ning it completely. One complete opening must bring a decrease in the superheat and
vice-versa. If the movement is reversed, check the electrical connections.
The superheat set point is too low Increase the superheat set point. Initially set it to 12 °C and check that there is no
longer return of liquid. Then gradually reduce the set point, always making sure there is
no return of liquid.
Low superheat protection ineective If the superheat remains low for too long with the valve that is slow to close, increase
the low superheat threshold and/or decrease the low superheat integral time. Initially
set the threshold 3 °C below the superheat set point, with an integral time of 3-4
seconds. Then gradually lower the low superheat threshold and increase the low
superheat integral time, checking that there is no return of liquid in any operating
conditions.
Stator broken or connected incorrectly Disconnect the stator from the valve and the cable and measure the resistance of the
windings using an ordinary tester.
The resistance of both should be around 36 ohms. Otherwise replace the stator. Finally,
check the electrical connections of the cable to the driver.
Valve stuck open Check if the superheating is always low (<2 °C) with the valve position permanently at
0 steps. If so, set the valve to manual control and close it completely. If the superheat is
always low, check the electrical connections and/or replace the valve.
The valve opening at start-up parameter
is too high on many showcases in which
the control set point is often reached (for
multiplexed showcases only)
Decrease the value of the Valve opening at start-up parameter on all the utilities,
making sure that there are no repercussions on the control temperature.
Liquid returns to the com-
pressor only after defrosting
(for multiplexed showcases
only)
The pause in control after defrosting is too
short (for MasterCase, MasterCase 2 and
mpxPRO only)
Increase the value of the valve control delay after defrosting” parameter.
The superheat temperature measured
by the driver after defrosting and before
reaching operating conditions is very low
for a few minutes
Check that the LowSH threshold is greater than the superheat value measured and that
the corresponding protection is activated (integral time > 0sec). If necessary, decrease
the value of the integral time.
The superheat temperature measured by
the driver does not reach low values, but
there is still return of liquid to the compres-
sor rack
Set more reactive parameters to bring forward the closing of the valve: increase the
proportional factor to 30, increase the integral time to 250 sec and increase the deriva-
tive time to 10 sec.
Many showcases defrosting at the same
time
Stagger the start defrost times. If this is not possible, if the conditions in the previous
two points are not present, increase the superheat set point and the LowSH thresholds
by at least 2 °C on the showcases involved.
The valve is signicantly oversized Replace the valve with a smaller equivalent.
Liquid returns to the com-
pressor only when starting
the controller (after being
OFF)
The valve opening at start-up parameter is
set too high
Check the calculation in reference to the ratio between the rated cooling capacity of
the evaporator and the capacity of the valve; if necessary, lower the value.
The superheat value swings
around the set point with an
amplitude greater than 4°C
The condensing pressure swings Check the controller condenser settings, giving the parameters “blander values (e.g.
increase the proportional band or increase the integral time). Note: the required
stability involves a variation within +/- 0.5 bars. If this is not eective or the settings
cannot be changed, adopt electronic valve control parameters for perturbed systems
(see paragraph 8.3)
The superheat swings even with the valve
set in manual control (in the position cor-
responding to the average of the working
values)
Check for the causes of the swings (e.g. low refrigerant charge) and resolve where pos-
sible. If not possible, adopt electronic valve control parameters for perturbed systems
(see paragraph 8.3).
The superheat does NOT swing with the
valve set in manual control (in the position
corresponding to the average of the
working values)
As a rst approach , decrease (by 30 to 50 %) the proportional factor. Subsequently
try increasing the integral time by the same percentage. In any case, adopt parameter
settings recommended for stable systems.
The superheat set point is too low Increase the superheat set point and check that the swings are reduced or disappear.
Initially set 13 °C, then gradually reduce the set point, making sure the system does not
start swinging again and that the unit temperature reaches the control set point.

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