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Cleaning the System
After a Compressor Burnout
Gildardo Yañez
ASHRAE
Distinguished Lecturer
www.gildardoyanez.com
What are the refrigeration system
contaminants?
The refrigeration system enemies
What are the refrigeration system
contaminants?
The disease of the refrigeration system
Refrigerant
Flood Back
Flooded
Start
Oil
Loss
Slugging Electrical
Failure
Mechanical
Failures
High
Temperature
High temperatures will make refrigerants lose
their thermal stability
• Refrigerant combustion, oil
combustion, crankcase heaters, etc.
– Organic Acids
– Phosgene
– Carbon Monoxide
– Carbon Dioxide
– Chlorine
The oil is a scavenger in the system
Contaminants in the system are a:
Until compressor dies
Recover the refrigerant
Push and pull connection is recommended
if you are going to recover more than 6 kg
Refrigerant Recovery Vapor Connection
Bad Practice
Recover the refrigerant in a non refillable cylinder
Effects of recovering refrigerant in a
non refillable cylinder
Effects of recovering refrigerant in a
non refillable cylinder
Refrigerant Recovery Cylinder
30 or 50 lbs
Recovering Refrigerant
• The compressor burnout will not
damage the refrigerant.
• The refrigerant can be recovered if the
contaminants are removed.
• Reference:
Cleaning Procedures
Page 26 B Exp (S1) 40-10
Sporlan
Blend Fractionation Test
1.Recover the refrigerant
Blend Fractionation Test
2. Cool down the recovery cylinder with ice
Blend Fractionation Test
If the pressure has a
5% up or down
variation the blend is
OK.
21 21.8 44.2 19.2 19.7 60.7 57.0 53.7 60.1
22 22.5 45.3 19.9 20.4 62.1 58.3 54.9 61.5
23 23.2 46.5 20.6 21.1 63.5 59.7 56.2 62.9
24 23.9 47.6 21.4 21.9 65.0 61.1 57.5 64.3
25 24.6 48.8 22.1 22.6 66.5 62.4 58.8 65.8
26 25.4 50.0 22.9 23.4 67.9 63.9 60.1 67.2
27 26.2 51.2 23.7 24.2 69.4 65.3 61.5 68.7
28 26.9 52.4 24.5 25.0 71.0 66.7 62.8 70.2
29 27.7 53.7 25.3 25.8 72.5 68.2 64.2 71.7
30 28.5 54.9 26.1 26.6 74.1 69.7 65.6 73.3
31 29.3 56.2 26.9 27.5 75.6 71.2 67.0 74.8
32 30.1 57.5 27.8 28.3 77.3 72.7 68.4 76.4
33 30.9 58.8 28.6 29.2 78.9 74.3 69.9 78.0
34 31.8 60.2 29.5 30.0 80.5 75.9 71.3 79.6
35 32.6 61.5 30.4 30.9 82.2 77.4 72.8 81.3
36 33.5 62.9 31.3 31.8 83.9 79.1 74.3 82.9
37 34.3 64.3 32.2 32.7 85.6 80.7 75.9 84.6
38 35.2 65.7 33.1 33.7 87.3 82.4 77.4 86.3
39 36.1 67.1 34.1 34.6 89.1 84.0 79.0 88.1
40 37.0 68.6 35.0 35.5 90.9 85.7 80.5 89.8
42 38.9 71.5 37.0 37.5 94.5 89.2 83.8 93.4
44 40.8 74.5 39.0 39.5 98.2 92.7 87.0 97.0
46 42.7 77.6 41.1 41.6 102.1 96.4 90.4 100.8
48 44.7 80.8 43.2 43.7 106.0 100.1 93.9 104.6
50 46.7 84.1 45.4 45.9 110.0 104.0 97.4 108.6
52 48.8 87.4 47.7 60.2 118.3 109.5 101.1 112.6
54 51.0 90.8 50.0 62.7 122.6 113.5 104.8 116.7
56 53.2 94.4 52.4 65.4 127.0 117.7 108.6 121.0
58 55.5 98.0 54.9 68.1 131.4 121.9 112.4 125.3
60 57.8 101.6 57.4 70.9 136.0 126.3 116.4 129.8
62 60.1 105.4 60.0 73.7 140.7 130.7 120.5 134.3
REFRIGERANTE (Código de letras Sporlan)
TEMP.
ºF CFC
12 (F)
HCFC
22 (V)
HFC
134a
(J)
HCFC
401A
(X)
HCFC
402A
(L)
HFC
404A
(S)
CFC
502 (R)
HFC
507 (P)
-60 19 .0 11.9 2 1.6 2 1.3 5 .6 6 .8 7 .2 5 .8
-55 17 .3 9 .2 2 0 .2 19 .9 1.9 3 .4 3 .9 2 .2
-50 15 .4 6 .1 18 .6 18 .2 1.0 0.2 0 .2 0.9
-45 13 .3 2 .7 16 .7 16 .3 3.2 2.3 1.9 3.1
-40 11.0 0.6 14 .7 14 .2 5.6 4.6 4.1 5.5
-38 10 .0 1.4 13 .8 13 .2 6.7 5.6 5.1 6.5
-36 8 .9 2.2 12 .8 12 .3 7.8 6.6 6.0 7.6
-34 7 .8 3.1 11.8 11.3 8.9 7.7 7.0 8.7
-32 6 .7 4.0 10 .8 10 .2 10.0 8.8 8.1 9.9
-30 5 .5 4.9 9 .7 9 .1 11.3 9.9 9.2 11.1
-28 4 .3 5.9 8 .6 7 .9 12.5 11.1 10.3 12.4
-26 3 .0 6.9 7 .4 6 .7 13.8 12.4 11.5 13.7
-24 1.6 8.0 6 .2 5 .5 15.2 13.6 12.7 15.0
-22 0 .3 9.1 4 .9 4 .2 16.6 15.0 14.0 16.4
-20 0.6 10.2 3 .6 2 .8 18.0 16.3 15.3 17.8
-18 1.3 11.4 2 .2 1.4 19.5 17.8 16.7 19.3
-16 2.1 12.6 0 .7 0.0 21.1 19.2 18.1 20.9
-14 2.8 13.9 0.4 0.8 22.7 20.8 19.5 22.5
-12 3.7 15.2 1.2 1.6 24.3 22.3 21.0 24.1
-10 4.5 16.5 2.0 2.4 26.0 24.0 22.6 25.8
40° F
Blend Fractionation Test
If the pressure is above 5%
of the expected pressure
you have non
condensable gases
40° F
21 21.8 44.2 19.2 19.7 60.7 57.0 53.7 60.1
22 22.5 45.3 19.9 20.4 62.1 58.3 54.9 61.5
23 23.2 46.5 20.6 21.1 63.5 59.7 56.2 62.9
24 23.9 47.6 21.4 21.9 65.0 61.1 57.5 64.3
25 24.6 48.8 22.1 22.6 66.5 62.4 58.8 65.8
26 25.4 50.0 22.9 23.4 67.9 63.9 60.1 67.2
27 26.2 51.2 23.7 24.2 69.4 65.3 61.5 68.7
28 26.9 52.4 24.5 25.0 71.0 66.7 62.8 70.2
29 27.7 53.7 25.3 25.8 72.5 68.2 64.2 71.7
30 28.5 54.9 26.1 26.6 74.1 69.7 65.6 73.3
31 29.3 56.2 26.9 27.5 75.6 71.2 67.0 74.8
32 30.1 57.5 27.8 28.3 77.3 72.7 68.4 76.4
33 30.9 58.8 28.6 29.2 78.9 74.3 69.9 78.0
34 31.8 60.2 29.5 30.0 80.5 75.9 71.3 79.6
35 32.6 61.5 30.4 30.9 82.2 77.4 72.8 81.3
36 33.5 62.9 31.3 31.8 83.9 79.1 74.3 82.9
37 34.3 64.3 32.2 32.7 85.6 80.7 75.9 84.6
38 35.2 65.7 33.1 33.7 87.3 82.4 77.4 86.3
39 36.1 67.1 34.1 34.6 89.1 84.0 79.0 88.1
40 37.0 68.6 35.0 35.5 90.9 85.7 80.5 89.8
42 38.9 71.5 37.0 37.5 94.5 89.2 83.8 93.4
44 40.8 74.5 39.0 39.5 98.2 92.7 87.0 97.0
46 42.7 77.6 41.1 41.6 102.1 96.4 90.4 100.8
48 44.7 80.8 43.2 43.7 106.0 100.1 93.9 104.6
50 46.7 84.1 45.4 45.9 110.0 104.0 97.4 108.6
52 48.8 87.4 47.7 60.2 118.3 109.5 101.1 112.6
54 51.0 90.8 50.0 62.7 122.6 113.5 104.8 116.7
56 53.2 94.4 52.4 65.4 127.0 117.7 108.6 121.0
58 55.5 98.0 54.9 68.1 131.4 121.9 112.4 125.3
60 57.8 101.6 57.4 70.9 136.0 126.3 116.4 129.8
62 60.1 105.4 60.0 73.7 140.7 130.7 120.5 134.3
REFRIGERANTE (Código de letras Sporlan)
TEMP.
ºF CFC
12 (F)
HCFC
22 (V)
HFC
134a
(J)
HCFC
401A
(X)
HCFC
402A
(L)
HFC
404A
(S)
CFC
502 (R)
HFC
507 (P)
-60 19 .0 11.9 2 1.6 2 1.3 5 .6 6 .8 7 .2 5 .8
-55 17 .3 9 .2 2 0 .2 19 .9 1.9 3 .4 3 .9 2 .2
-50 15 .4 6 .1 18 .6 18 .2 1.0 0.2 0 .2 0.9
-45 13 .3 2 .7 16 .7 16 .3 3.2 2.3 1.9 3.1
-40 11.0 0.6 14 .7 14 .2 5.6 4.6 4.1 5.5
-38 10 .0 1.4 13 .8 13 .2 6.7 5.6 5.1 6.5
-36 8 .9 2.2 12 .8 12 .3 7.8 6.6 6.0 7.6
-34 7 .8 3.1 11.8 11.3 8.9 7.7 7.0 8.7
-32 6 .7 4.0 10 .8 10 .2 10.0 8.8 8.1 9.9
-30 5 .5 4.9 9 .7 9 .1 11.3 9.9 9.2 11.1
-28 4 .3 5.9 8 .6 7 .9 12.5 11.1 10.3 12.4
-26 3 .0 6.9 7 .4 6 .7 13.8 12.4 11.5 13.7
-24 1.6 8.0 6 .2 5 .5 15.2 13.6 12.7 15.0
-22 0 .3 9.1 4 .9 4 .2 16.6 15.0 14.0 16.4
-20 0.6 10.2 3 .6 2 .8 18.0 16.3 15.3 17.8
-18 1.3 11.4 2 .2 1.4 19.5 17.8 16.7 19.3
-16 2.1 12.6 0 .7 0.0 21.1 19.2 18.1 20.9
-14 2.8 13.9 0.4 0.8 22.7 20.8 19.5 22.5
-12 3.7 15.2 1.2 1.6 24.3 22.3 21.0 24.1
-10 4.5 16.5 2.0 2.4 26.0 24.0 22.6 25.8
Better safe than sorry
Remove the compressor carefully
• Remove the burned compressor
• Be aware that the system can be acid contaminated
• Do not touch oil with your bare hands
• Avoid breathing the acid vapors
You need to know what went wrong?
Before you install the new compressor
1.- Refrigerant Floodback
2.- Flooded Starts
3.- Slugging
4.- Compressor Overheating
5.- Electrical Failure
Any Ideas?Refrigerant Flooback / Moisture in the System
Remove the accesories from the
system
• Such as:
• Liquid Line and
Suction Filters
• Liquid indicators
• Metering devices
• Solenoid Valves
• Manual Valves
• Oil Separator
Purge the system with nitrogen
Open
Open
Open
2 to 3
psig
Bad Practice
Avoid the use of R-141b & R-22 as a cleaning agent
Install a new thermostatic valve
Clean all the accessories
Install a new thermostatic valve
Or install a new metering device
Install a big liquid line filter
• This should be the
largest you can
install.
Activated Carbon Filter
If the system is above 40 tons
This filter removes:
Oil Sludge, neutralizes
acid in the system, and
also removes debriefs
from the motor burnout.
The carbon activated
filter or core is the one
you should install
Permanent Suction Line Filter / Drier-Filter
If the system is up to 40 tons
This filter is made of a
blended mixture of activaded alumina and molecular sieves
Brazing type
suction filter
Liquid line sight glass
(Moisture Indicator)
• This accessory will help us know when we need
to change the cores filters.
Oil Separator
Install a new oil separator
It is very possible that you will find debriefs of compressor in it
Oil Separator
Compressor debriefs at the bottom
Contaminated Oil with metal
Non condensable gases effects
• If you leave non condensable
gases in the system they will cause:
1. High temperature in the high side
pressure.
2. The high pressure valve will become
very hot
3. Organic acids will form.
4. They will cause a early compressor
failure.
Moisture presence in the system
1. It will cause ice presence.
2. Ice will block the system metering
devices in the system such as:
• Cap tubes
• Thermostatic Expansion Valves
3. System problems.
4. It might damage internal compressor
parts.
When TEV is closed
• High temperature side very hot.
• High superheat at the compressor.
• Suction pressure lower than usual.
When TEV is wide open
• Cause Refrigerant Flood Back into to
the compressor crankase
• Low Super heat at the compressor.
• Suction pressure, unsual higher
suction pressure.
• These two contaminants will cause a
chemical reaction that will form:
1. Organic Acids
2. Oil Sludge
• Will cause early failures
in the compressors.
What happens if I pull the vacumm with the
compressor?
 The motor insulation will be damaged
since the start up.
1. The motor windings work with out cooling,
that will cause damage to the motor
insulation.
2. The windings will short because of heat and
because the motor is working in a vacuum
environment condition.
How to select the right vacuum pump?
1. You need to know the refrigeration
tons’ capacity of the system.
2. Thumb Rule: 1 cfm can dehydrate a 7
refrigeration tons system.
3. Now you are ready to select
the right vacuum capacity.
Example
• 30 R.T. Chiller
• The recomended
vacuum pump will
be:
– 6 CFM x 7 = 42 Tons
– 4 CFM x 7 = 28 Tons
Vacuum Meassuremt
Bad Refigeration Practice
Pull a deep vacuum, using the service manifold to measure it.
Copeland Application Engineering Bulletin
Process
» Connect your vacuum pump
to the system
» Start the vacuum pump
» We stop when reach 1500
microns
» Break the vacuum with
nitrogen and pressurize the
system up to 2 psig.
» Wait 30 minutes
Triple Evacuation Process
Step 1
2 psig
The vacuum pump must be connected to both the high
and low sides of the system through adequate
connections
Accelerate the speed of the vacuum
Purging with nitrogen dries the system
Open
Open
Open
2 to 3
psig
Better safe than sorry
The nitrogen tank must have a pressure-regulating valve
Never attempt to pressurize a system without first
installing an appropriate pressure-regulating valve.
• The vacuum pump oil will turn white
• Open the vacuum pump gas ballast
• Wait until the oil slowly restores to its
usual state
• Close the gas ballast valve
Copeland Application Engineering Bulletin
2 psig
Triple Evacuation Process
Step 2
» Vent the nitrogen from the
system
» Connect your vacuum pump to
the system
» Start the vacuum pump
» We stop when reach 1500
microns
» Break the vacuum with nitrogen
and pressurize the system up to
2 psig.
» We wait 30 minutes
Copeland Application Engineering Bulletin
» Vent the nitrogen from the
system
» Connect your vacuum pump to
the system
» Start the vacuum pump
» Stop your pump when you reach
500 or 250 microns, depending
the type of lubricant
» Break the vacuum with
refrigerant
Triple Evacuation Process
Step 3
Why the moisture is eliminated from the
system?
•The system pressure drops down
•The water boiling point changes
•The ambient temperature remains the same
For how long?
• You cannot measure vacuum with time
• External conditions that affect vacuum
time:
– Meters above the sea level
– System or equipment temperature
– Hose diameter
– Hose length
– Manifold location
Copeland Compressor Operation & Service
Semminar 1998
Deep Vacuum Level
Charge the system with refrigerant
• Decide if you are
reusing the recovered
refrigerant of the
system.
• Charging metods:
– By Superheat
– By Weight
Charging measuring Superheat
• Start the system
• Wait until the system
stabilizes
• Check the superheat
• Example:
• Suction Line Temp: 44°F
• Evaporating Temp: 34°F
• Superheat: 10°F
Check the system while is operating
An oil sample should be taken every
24 running hours
• Then the oil
• The filter-driers
• Or both may be
changed.
• Depending upon
results of the oil
test.
Blocked Filter-Drier
Blocked Filter-Drier
Keep taking oil samples every
24 running hours
• Until you are sure the
acid level dropped
down
Simultaneously you need to check:
1. Acid level
2. System pressure
3. Moisture level using the sight glass moisture indicator
Secure the running conditions
Be sure the running conditions are already
stabilized
After 2 weeks a visit to the system
is recommended
When you visit the system after 2
weeks check:
Cleaning the System
After a Compressor Burnout
Gildardo Yañez
ASHRAE
Distinguished Lecturer
www.gildardoyanez.com

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Refrigeration system cleaning

  • 1. Cleaning the System After a Compressor Burnout Gildardo Yañez ASHRAE Distinguished Lecturer www.gildardoyanez.com
  • 2. What are the refrigeration system contaminants? The refrigeration system enemies
  • 3. What are the refrigeration system contaminants? The disease of the refrigeration system
  • 5. High temperatures will make refrigerants lose their thermal stability • Refrigerant combustion, oil combustion, crankcase heaters, etc. – Organic Acids – Phosgene – Carbon Monoxide – Carbon Dioxide – Chlorine
  • 6. The oil is a scavenger in the system
  • 7. Contaminants in the system are a:
  • 9. Recover the refrigerant Push and pull connection is recommended if you are going to recover more than 6 kg
  • 11. Bad Practice Recover the refrigerant in a non refillable cylinder
  • 12. Effects of recovering refrigerant in a non refillable cylinder
  • 13. Effects of recovering refrigerant in a non refillable cylinder
  • 15. Recovering Refrigerant • The compressor burnout will not damage the refrigerant. • The refrigerant can be recovered if the contaminants are removed. • Reference: Cleaning Procedures Page 26 B Exp (S1) 40-10 Sporlan
  • 16.
  • 17.
  • 18.
  • 20. Blend Fractionation Test 2. Cool down the recovery cylinder with ice
  • 21. Blend Fractionation Test If the pressure has a 5% up or down variation the blend is OK. 21 21.8 44.2 19.2 19.7 60.7 57.0 53.7 60.1 22 22.5 45.3 19.9 20.4 62.1 58.3 54.9 61.5 23 23.2 46.5 20.6 21.1 63.5 59.7 56.2 62.9 24 23.9 47.6 21.4 21.9 65.0 61.1 57.5 64.3 25 24.6 48.8 22.1 22.6 66.5 62.4 58.8 65.8 26 25.4 50.0 22.9 23.4 67.9 63.9 60.1 67.2 27 26.2 51.2 23.7 24.2 69.4 65.3 61.5 68.7 28 26.9 52.4 24.5 25.0 71.0 66.7 62.8 70.2 29 27.7 53.7 25.3 25.8 72.5 68.2 64.2 71.7 30 28.5 54.9 26.1 26.6 74.1 69.7 65.6 73.3 31 29.3 56.2 26.9 27.5 75.6 71.2 67.0 74.8 32 30.1 57.5 27.8 28.3 77.3 72.7 68.4 76.4 33 30.9 58.8 28.6 29.2 78.9 74.3 69.9 78.0 34 31.8 60.2 29.5 30.0 80.5 75.9 71.3 79.6 35 32.6 61.5 30.4 30.9 82.2 77.4 72.8 81.3 36 33.5 62.9 31.3 31.8 83.9 79.1 74.3 82.9 37 34.3 64.3 32.2 32.7 85.6 80.7 75.9 84.6 38 35.2 65.7 33.1 33.7 87.3 82.4 77.4 86.3 39 36.1 67.1 34.1 34.6 89.1 84.0 79.0 88.1 40 37.0 68.6 35.0 35.5 90.9 85.7 80.5 89.8 42 38.9 71.5 37.0 37.5 94.5 89.2 83.8 93.4 44 40.8 74.5 39.0 39.5 98.2 92.7 87.0 97.0 46 42.7 77.6 41.1 41.6 102.1 96.4 90.4 100.8 48 44.7 80.8 43.2 43.7 106.0 100.1 93.9 104.6 50 46.7 84.1 45.4 45.9 110.0 104.0 97.4 108.6 52 48.8 87.4 47.7 60.2 118.3 109.5 101.1 112.6 54 51.0 90.8 50.0 62.7 122.6 113.5 104.8 116.7 56 53.2 94.4 52.4 65.4 127.0 117.7 108.6 121.0 58 55.5 98.0 54.9 68.1 131.4 121.9 112.4 125.3 60 57.8 101.6 57.4 70.9 136.0 126.3 116.4 129.8 62 60.1 105.4 60.0 73.7 140.7 130.7 120.5 134.3 REFRIGERANTE (Código de letras Sporlan) TEMP. ºF CFC 12 (F) HCFC 22 (V) HFC 134a (J) HCFC 401A (X) HCFC 402A (L) HFC 404A (S) CFC 502 (R) HFC 507 (P) -60 19 .0 11.9 2 1.6 2 1.3 5 .6 6 .8 7 .2 5 .8 -55 17 .3 9 .2 2 0 .2 19 .9 1.9 3 .4 3 .9 2 .2 -50 15 .4 6 .1 18 .6 18 .2 1.0 0.2 0 .2 0.9 -45 13 .3 2 .7 16 .7 16 .3 3.2 2.3 1.9 3.1 -40 11.0 0.6 14 .7 14 .2 5.6 4.6 4.1 5.5 -38 10 .0 1.4 13 .8 13 .2 6.7 5.6 5.1 6.5 -36 8 .9 2.2 12 .8 12 .3 7.8 6.6 6.0 7.6 -34 7 .8 3.1 11.8 11.3 8.9 7.7 7.0 8.7 -32 6 .7 4.0 10 .8 10 .2 10.0 8.8 8.1 9.9 -30 5 .5 4.9 9 .7 9 .1 11.3 9.9 9.2 11.1 -28 4 .3 5.9 8 .6 7 .9 12.5 11.1 10.3 12.4 -26 3 .0 6.9 7 .4 6 .7 13.8 12.4 11.5 13.7 -24 1.6 8.0 6 .2 5 .5 15.2 13.6 12.7 15.0 -22 0 .3 9.1 4 .9 4 .2 16.6 15.0 14.0 16.4 -20 0.6 10.2 3 .6 2 .8 18.0 16.3 15.3 17.8 -18 1.3 11.4 2 .2 1.4 19.5 17.8 16.7 19.3 -16 2.1 12.6 0 .7 0.0 21.1 19.2 18.1 20.9 -14 2.8 13.9 0.4 0.8 22.7 20.8 19.5 22.5 -12 3.7 15.2 1.2 1.6 24.3 22.3 21.0 24.1 -10 4.5 16.5 2.0 2.4 26.0 24.0 22.6 25.8 40° F
  • 22. Blend Fractionation Test If the pressure is above 5% of the expected pressure you have non condensable gases 40° F 21 21.8 44.2 19.2 19.7 60.7 57.0 53.7 60.1 22 22.5 45.3 19.9 20.4 62.1 58.3 54.9 61.5 23 23.2 46.5 20.6 21.1 63.5 59.7 56.2 62.9 24 23.9 47.6 21.4 21.9 65.0 61.1 57.5 64.3 25 24.6 48.8 22.1 22.6 66.5 62.4 58.8 65.8 26 25.4 50.0 22.9 23.4 67.9 63.9 60.1 67.2 27 26.2 51.2 23.7 24.2 69.4 65.3 61.5 68.7 28 26.9 52.4 24.5 25.0 71.0 66.7 62.8 70.2 29 27.7 53.7 25.3 25.8 72.5 68.2 64.2 71.7 30 28.5 54.9 26.1 26.6 74.1 69.7 65.6 73.3 31 29.3 56.2 26.9 27.5 75.6 71.2 67.0 74.8 32 30.1 57.5 27.8 28.3 77.3 72.7 68.4 76.4 33 30.9 58.8 28.6 29.2 78.9 74.3 69.9 78.0 34 31.8 60.2 29.5 30.0 80.5 75.9 71.3 79.6 35 32.6 61.5 30.4 30.9 82.2 77.4 72.8 81.3 36 33.5 62.9 31.3 31.8 83.9 79.1 74.3 82.9 37 34.3 64.3 32.2 32.7 85.6 80.7 75.9 84.6 38 35.2 65.7 33.1 33.7 87.3 82.4 77.4 86.3 39 36.1 67.1 34.1 34.6 89.1 84.0 79.0 88.1 40 37.0 68.6 35.0 35.5 90.9 85.7 80.5 89.8 42 38.9 71.5 37.0 37.5 94.5 89.2 83.8 93.4 44 40.8 74.5 39.0 39.5 98.2 92.7 87.0 97.0 46 42.7 77.6 41.1 41.6 102.1 96.4 90.4 100.8 48 44.7 80.8 43.2 43.7 106.0 100.1 93.9 104.6 50 46.7 84.1 45.4 45.9 110.0 104.0 97.4 108.6 52 48.8 87.4 47.7 60.2 118.3 109.5 101.1 112.6 54 51.0 90.8 50.0 62.7 122.6 113.5 104.8 116.7 56 53.2 94.4 52.4 65.4 127.0 117.7 108.6 121.0 58 55.5 98.0 54.9 68.1 131.4 121.9 112.4 125.3 60 57.8 101.6 57.4 70.9 136.0 126.3 116.4 129.8 62 60.1 105.4 60.0 73.7 140.7 130.7 120.5 134.3 REFRIGERANTE (Código de letras Sporlan) TEMP. ºF CFC 12 (F) HCFC 22 (V) HFC 134a (J) HCFC 401A (X) HCFC 402A (L) HFC 404A (S) CFC 502 (R) HFC 507 (P) -60 19 .0 11.9 2 1.6 2 1.3 5 .6 6 .8 7 .2 5 .8 -55 17 .3 9 .2 2 0 .2 19 .9 1.9 3 .4 3 .9 2 .2 -50 15 .4 6 .1 18 .6 18 .2 1.0 0.2 0 .2 0.9 -45 13 .3 2 .7 16 .7 16 .3 3.2 2.3 1.9 3.1 -40 11.0 0.6 14 .7 14 .2 5.6 4.6 4.1 5.5 -38 10 .0 1.4 13 .8 13 .2 6.7 5.6 5.1 6.5 -36 8 .9 2.2 12 .8 12 .3 7.8 6.6 6.0 7.6 -34 7 .8 3.1 11.8 11.3 8.9 7.7 7.0 8.7 -32 6 .7 4.0 10 .8 10 .2 10.0 8.8 8.1 9.9 -30 5 .5 4.9 9 .7 9 .1 11.3 9.9 9.2 11.1 -28 4 .3 5.9 8 .6 7 .9 12.5 11.1 10.3 12.4 -26 3 .0 6.9 7 .4 6 .7 13.8 12.4 11.5 13.7 -24 1.6 8.0 6 .2 5 .5 15.2 13.6 12.7 15.0 -22 0 .3 9.1 4 .9 4 .2 16.6 15.0 14.0 16.4 -20 0.6 10.2 3 .6 2 .8 18.0 16.3 15.3 17.8 -18 1.3 11.4 2 .2 1.4 19.5 17.8 16.7 19.3 -16 2.1 12.6 0 .7 0.0 21.1 19.2 18.1 20.9 -14 2.8 13.9 0.4 0.8 22.7 20.8 19.5 22.5 -12 3.7 15.2 1.2 1.6 24.3 22.3 21.0 24.1 -10 4.5 16.5 2.0 2.4 26.0 24.0 22.6 25.8
  • 23. Better safe than sorry Remove the compressor carefully • Remove the burned compressor • Be aware that the system can be acid contaminated • Do not touch oil with your bare hands • Avoid breathing the acid vapors
  • 24. You need to know what went wrong? Before you install the new compressor 1.- Refrigerant Floodback 2.- Flooded Starts 3.- Slugging 4.- Compressor Overheating 5.- Electrical Failure
  • 25.
  • 26.
  • 27.
  • 28.
  • 29.
  • 30. Any Ideas?Refrigerant Flooback / Moisture in the System
  • 31. Remove the accesories from the system • Such as: • Liquid Line and Suction Filters • Liquid indicators • Metering devices • Solenoid Valves • Manual Valves • Oil Separator
  • 32. Purge the system with nitrogen Open Open Open 2 to 3 psig
  • 33. Bad Practice Avoid the use of R-141b & R-22 as a cleaning agent
  • 34. Install a new thermostatic valve Clean all the accessories Install a new thermostatic valve Or install a new metering device
  • 35. Install a big liquid line filter • This should be the largest you can install.
  • 36. Activated Carbon Filter If the system is above 40 tons This filter removes: Oil Sludge, neutralizes acid in the system, and also removes debriefs from the motor burnout. The carbon activated filter or core is the one you should install
  • 37.
  • 38. Permanent Suction Line Filter / Drier-Filter If the system is up to 40 tons This filter is made of a blended mixture of activaded alumina and molecular sieves Brazing type suction filter
  • 39. Liquid line sight glass (Moisture Indicator) • This accessory will help us know when we need to change the cores filters.
  • 40. Oil Separator Install a new oil separator It is very possible that you will find debriefs of compressor in it
  • 41.
  • 42.
  • 44.
  • 46.
  • 47.
  • 48.
  • 49. Non condensable gases effects • If you leave non condensable gases in the system they will cause: 1. High temperature in the high side pressure. 2. The high pressure valve will become very hot 3. Organic acids will form. 4. They will cause a early compressor failure.
  • 50.
  • 51.
  • 52.
  • 53.
  • 54.
  • 55.
  • 56.
  • 57. Moisture presence in the system 1. It will cause ice presence. 2. Ice will block the system metering devices in the system such as: • Cap tubes • Thermostatic Expansion Valves 3. System problems. 4. It might damage internal compressor parts.
  • 58. When TEV is closed • High temperature side very hot. • High superheat at the compressor. • Suction pressure lower than usual.
  • 59. When TEV is wide open • Cause Refrigerant Flood Back into to the compressor crankase • Low Super heat at the compressor. • Suction pressure, unsual higher suction pressure.
  • 60.
  • 61.
  • 62. • These two contaminants will cause a chemical reaction that will form: 1. Organic Acids 2. Oil Sludge • Will cause early failures in the compressors.
  • 63.
  • 64.
  • 65.
  • 66.
  • 67. What happens if I pull the vacumm with the compressor?  The motor insulation will be damaged since the start up. 1. The motor windings work with out cooling, that will cause damage to the motor insulation. 2. The windings will short because of heat and because the motor is working in a vacuum environment condition.
  • 68.
  • 69.
  • 70.
  • 71. How to select the right vacuum pump? 1. You need to know the refrigeration tons’ capacity of the system. 2. Thumb Rule: 1 cfm can dehydrate a 7 refrigeration tons system. 3. Now you are ready to select the right vacuum capacity.
  • 72. Example • 30 R.T. Chiller • The recomended vacuum pump will be: – 6 CFM x 7 = 42 Tons – 4 CFM x 7 = 28 Tons
  • 74. Bad Refigeration Practice Pull a deep vacuum, using the service manifold to measure it.
  • 75. Copeland Application Engineering Bulletin Process » Connect your vacuum pump to the system » Start the vacuum pump » We stop when reach 1500 microns » Break the vacuum with nitrogen and pressurize the system up to 2 psig. » Wait 30 minutes Triple Evacuation Process Step 1 2 psig
  • 76.
  • 77. The vacuum pump must be connected to both the high and low sides of the system through adequate connections
  • 78. Accelerate the speed of the vacuum
  • 79. Purging with nitrogen dries the system Open Open Open 2 to 3 psig
  • 80. Better safe than sorry The nitrogen tank must have a pressure-regulating valve Never attempt to pressurize a system without first installing an appropriate pressure-regulating valve.
  • 81. • The vacuum pump oil will turn white • Open the vacuum pump gas ballast • Wait until the oil slowly restores to its usual state • Close the gas ballast valve
  • 82.
  • 83. Copeland Application Engineering Bulletin 2 psig Triple Evacuation Process Step 2 » Vent the nitrogen from the system » Connect your vacuum pump to the system » Start the vacuum pump » We stop when reach 1500 microns » Break the vacuum with nitrogen and pressurize the system up to 2 psig. » We wait 30 minutes
  • 84. Copeland Application Engineering Bulletin » Vent the nitrogen from the system » Connect your vacuum pump to the system » Start the vacuum pump » Stop your pump when you reach 500 or 250 microns, depending the type of lubricant » Break the vacuum with refrigerant Triple Evacuation Process Step 3
  • 85. Why the moisture is eliminated from the system? •The system pressure drops down •The water boiling point changes •The ambient temperature remains the same
  • 86. For how long? • You cannot measure vacuum with time • External conditions that affect vacuum time: – Meters above the sea level – System or equipment temperature – Hose diameter – Hose length – Manifold location
  • 87. Copeland Compressor Operation & Service Semminar 1998 Deep Vacuum Level
  • 88. Charge the system with refrigerant • Decide if you are reusing the recovered refrigerant of the system. • Charging metods: – By Superheat – By Weight
  • 89. Charging measuring Superheat • Start the system • Wait until the system stabilizes • Check the superheat • Example: • Suction Line Temp: 44°F • Evaporating Temp: 34°F • Superheat: 10°F
  • 90. Check the system while is operating
  • 91. An oil sample should be taken every 24 running hours • Then the oil • The filter-driers • Or both may be changed. • Depending upon results of the oil test.
  • 94.
  • 95.
  • 96. Keep taking oil samples every 24 running hours • Until you are sure the acid level dropped down
  • 97. Simultaneously you need to check: 1. Acid level 2. System pressure 3. Moisture level using the sight glass moisture indicator
  • 98. Secure the running conditions
  • 99. Be sure the running conditions are already stabilized After 2 weeks a visit to the system is recommended
  • 100. When you visit the system after 2 weeks check:
  • 101.
  • 102. Cleaning the System After a Compressor Burnout Gildardo Yañez ASHRAE Distinguished Lecturer www.gildardoyanez.com

Editor's Notes

  1. Limpieza de Sistemas
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