Industrial refrigerant machine operators seem to be simple people within the production chain but essentially are very important. Take up the quiz below and see how good you are as a refrigerant machine operator. This test consists of 100 most important questions that will help you clear the certification exam of the same. All the best.
INCREASE CAPACITY
STOP FLOW OF REFRIGERANT WITHOUT STOPPING
REDUCE CAPACITY
START FLOW OF REFRIGERANT THROUGH SYSTEM
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ARE FULLY ENCLOSED AND CANNOT BE SERVICED ON SITE
ARE EASIER TO GET TO
ARE MORE DIFFICULT TO GET TO
ARE MORE EXPENSIVE
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SCALE PARTICLES LODGED IN THE TEV VALVE
UNRAVELING OF THE INSULATION PROTECTING THE TEV VALVE THERMAL BULB
BUILD-UP OF NONCONDENSABLES IN THE CONDENSER
OVERCHARGE OF REFRIGERANT
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THE HIGH PRESSURE CUT IN
THE LOW SIDE PRESSURE STAT
THE THERMOSTATIC EXPANSION VALVE
THE THERMOSTAT THAT ACTIVATES THE SOLENOID VALVE
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FAULTY MACHINE CONTROL
PROPER REFRIGERATION CHARGE
FAULTY COMPRESSOR VALVES
POOR CONDENSER OPERATION / DIRTY TUBES
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A1
A2
B2
B3
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MUST ENSURE THE FLAME IS ENCLOSED AND VENTED TO OPEN AIR
MAY MAKE REPAIRS AT LEAST 25 FEET FROM THE REFRIGERANT UNIT
MAY MAKE REPAIRS WITHOUT ANY RESTRICTIONS IF THE REFRIGERATING UNIT IS SHUT DOWN
MAY NOT MAKE REPAIR UNDER ANY CIRCUMSTANCES
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BYPASS DISCHARGE GAS
ADJUSTMENT OF THE IMPELLER INLET GUIDE PRE-ROTATION VANES
CONDENSER PRESSURE VARIATION
ADDING RE-EXPANSION VOLUME
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SOLENOID VALVE
HIGH SIDE FLOAT
THERMAL EXPANSION VALVE
CAPILLARY TUBE
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FILTER SUCTION AND DISCHARGE VALVES
SUCTION VALVE AND DISCHARGE BYPASS BOTH OPEN
SUCTION BYPASS AND DISCHARGE VALVE BOTH OPEN
DISCHARGE BYPASS AND SUCTION VALVE BOTH CLOSED
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OPENING THE SUCTION VALVES WITH SOME FORM OF CONTROL
CONTROLLING THE DISCHARGE PRESSURE
CHANGING THE STROKE AND ADDING RE-EXPANSION VOLUME
RETURNING THE DISCHARGE GAS TO SUCTION
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INCREASING THE AMOUNT OF SUPERHEAT
INCREASING THE AMOUNT OF SUB-COOLING
DECREASE THE AMOUNT OF SUPERHEAT
DECREASE THE AMOUNT OF SUB-COOLING
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HIGH COOLING WATER BEING RETURNED
RISE IN CONDENSER HEAD PRESSURE
LOWER COOLING WATER TEMPERATURE RETURN
NO NOTICEABLE EFFECT OF THE COOLING TOWER TEMP BEING RETURNED
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DECREASE IN SUPER HEAT TEMP ENTERING COMPRESSOR
AN INCREASE IN COMPRESSOR HEAD PRESSURE
AN INCREASE IN THE FLOW RATE OF NONCONDENSABLES
CONDENSER TO METERING DEVICE FROZEN
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TO COOL THE REFRIGERANT
TO STORE EXCESS REFRIGERANT
TO FILTER IMPURITIES FROM THE REFRIGERANT
TO INCREASE COMPRESSOR EFFICIENCY
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5% OVER DESIGN PRESSURE
THE DESIGN PRESSURE
RECOMMENDED OPERATING PRESSURE FOR NORMAL COOLING CONDITIONS
20% BELOW DESIGN PRESSURE
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HIGH AND LOW VALVES BACKSEATED
HIGH AND LOW VALVES FRONTSEATED
HIGH SIDE BACKSEATED, LOW SIDE FRONTSEATED
HIGH SIDE FRONTSEATED, LOW SIDE BACKSEATED
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SOLENOID VALVE, SIGHT-GLASS, AND DRIER
DRIER, SIGHT-GLASS, AND SOLENOID VALVE
DRIER, SOLENOID VALVE, AND SIGHT-GLASS
NONE OF THE ABOVE
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NOT ENOUGH REFRIGERANT IN SYSTEM
EXPANSION VALVE OPEN TOO WIDE
THE COMPRESSOR IS RUNNING CONTINUALLY
COMPRESSOR VALVES ARE LEAKING
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ORANGE
GREEN
YELLOW
WHITE
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80°F
90°F
110°F
130°F
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60 LBS
45 LBS
30 LBS
15 LBS
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STARVED EVAPORATOR
LEAK IN SYSTEM
LOW REFRIGERANT CHARGE
ANY OF THE ABOVE
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LIGHT SUCTION VALVE SPRINGS
HIGH SUCTION PRESSURE
LEAK IN THE SUCTION VALVE
LOW SUCTION PRESSURE
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VAPOR RECYCLING UNIT
AN ECONOMIZER
REFRIGERANT CLEANER
EVAPORATOR
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A1
B2
A3
B1
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HIGH PRESSURE GAS AND LEAVES AS LOW PRESSURE LIQUID
HIGH PRESSURE GAS AND LEAVES AS HIGH PRESSURE LIQUID
SUPERHEATED GAS AND LEAVES AS HIGH TEMPERATURE LIQUID
HIGH TEMPERATURE GAS AND LEAVES AS SUPERHEATED GAS
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GROUP 2, B2
GROUP 1, A1
GROUP 3, B1
BOTH A1 AND B1
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GROUP 1
GROUP 2
GROUP 3
GROUP 4
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RECIPROCATING
ROTORY, SCREW
SCROLL
CENTRIFUGAL
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DAMAGE TO FAN BLADES
INCREASE IN COOLING TOWER WATER TEMP BEING RETURNED
DECREASE IN MAKEUP WATER REQUIREMENTS
A DROP IN WET BULB TEMP
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7.7
0.6
5.9
23.5
HEAD PSI DROPPING TO LOW
DECREASE THE CAPACITY OF THE COMPRESSOR AND REFRIGERATION SYSTEM
NON-CONDENSABLES ARE MORE PRONE TO COLLECT IN THE SYSTEM
FROST MAY DEVELOP IN THE SUCTION LINE
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REDUCE BY 1/2
INCREASE BY A FACTOR OF 2
STAY THE SAME
INCREASE BY A FACTOR OF 4
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36
30
24
32
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WATER, OIL, REFRIGERANT
OIL, REFRIGERANT, WATER
REFRIGERANT, OIL, WATER
OIL, WATER, REFRIGERANT
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HIGH PRESSURE SIDE OF THE EQUIPMENT
LOW PRESSURE SIDE OF THE EQUIPMENT
DISCHARGE SIDE OF THE EQUIPMENT
RECIEVER
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SPECIFIC HEAT
SUPER HEAT
LATENT HEAT
SENSIBLE HEAT
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113
313
213
13
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PURGE AT RAPID RATE
PURGE WITH COMPRESSOR ON
STOP WHEN PRESSURE CEASES TO DROP
RUN THE CONDENSER AS MUCH AS POSSIBLE
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1204
1002
1808
1406
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CONDENSER
ECONOMIZER
COMPRESSOR DISCHARGE
EVAPORATOR
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32
28
40
18
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AS HEAT OF EVAPORATION OF THE COOLING TOWER
IN THE ECONOMIZER
IN THE EVAPORATOR
CONDENSER WATER OUTLET
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SLUGGING COMPRESSOR
FLOODED EVAPORATOR
STARVED EVAPORATOR
UNINSULATED SUCTION LINE
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REDUCING PRESSURE
RAISING PRESSURE
REGULATING PRESSURE
STABILIZING PRESSURE
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STARVE
FLOOD
INCREASE SUPERHEAT
RESPOND NORMALLY
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277 FEET
1,440 INCHES
1,440 FEET
277 INCHES
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