Q1 What is the difference
between Molecular sieve
and Silica gel drier?
The non crystalline silica
gel does not have as
much water adsorbing
capability as the Molecular
sieve at the temperatures
encountered in refrigeration.
Also that Silica gel
adsorbs some of the lubricating
oil and refrigerant also
in addition to the water
molecules because of
larger pore sizes as
compared to Molecular
sieve which have smaller
pores and adsorb only
water molecules. Further
as compared to molecular
sieves, silica gel has
less strength and can
shatter when contacted
by liquid water and when
subjected to repeated
freeze thaw cycles. This
leads to capillary chokes.
Apart from the above
reasons, the weight of
silica gel to be used
to reduce a R12 system's
moisture level will have
to be about over 5 to
6 times the weight of
the molecular sieve needed
for the same purpose.
Q2 Why silica gel is not
recommended for R134a?
In fact silica gel is
not recommended even
for R12 on account of
the reasons mentioned
above. In the early days
before molecular sieves
were developed, silica
gel was used and continues
to be used in servicing
but not by any reputed
Appliance OEM even for
R12.
Q3 What is the specification
of XH-7/XH-9 other than
that of molecular sieve?
XH7 & XH9 indicate
the type of molecular
sieves made by UOP (US
manufacturer) that use
the brand name MOLSIV
and the desiccants are
designated by them as
MOLSIV 4A- XH 7, MOLSIV
4A- XH9, MOLSIV 4A- XH5,
MOLSIV 4A-XH6. The prefix
4A is used by most molecular
sieve manufacturers and
indicates that the size
of the pores in the molecular
sieve is 4 Angstrom or
0.4 nm (nano meters).
The suffix XH 5 etc are
the designations given
by UOP to the molecular
sieves developed by them.
The higher the numbers
following XH indicates
a newer development and
is also indicative of
higher hydrated attrition
strength (particularly
XH7 & XH9) needed
for 134a.
Other specifications
applicable to most desiccants
also apply to molecular
sieves; these being,
Water capacity, Bead
size (usually 1/16" for
mol sieves and 1/8" for
activated alumina and
silica gel), crush strength,
attrition strength both
dry and hydrated.
Q4 If both XH7 & XH9
are suitable for 134a
what is the difference
between the two?
XH7 was first developed
for 134a for Auto AC
systems after it was
found that the existing
XH5 used in R12 systems
reacted chemically with
134a, apart from lower
hydrated attrition strength.
It was found to be ok
for both auto AC and
stationary systems as
well as with R12. However
it is not recommended
for R22 systems. XH9
was subsequently developed
as a more versatile product
suitable for all 134a,
R12, R22, HFCs 125,143a & 152a.
Q5 What is the
specification of XH5
used in R12 & HC
systems?
Specifications are covered
under Question-3 above.
XH5 can be used in R12 & HC
systems. However it is
not recommended for R22.
Infact for R22, both
XH5 & XH7 are unsuitable
and either 4A XH6 or
4A XH9 are to be used.
Q6 What is the structural
difference in the filter
drier used in CFC and
HFC appliance?
XH5 can be used for R12 & HC
systems; XH7 and XH9
are used for R134a systems.
These are molecular sieves,
higher the number following
XH indicates a newer
development and is also
indicative of higher
hydrated attrition strength.
For a given quantity
of molecular sieve XH7
or XH9 will have more
surface area than XH5
to adsorb water.
Q7 Can we use drier with
silica gel as desiccant
for R134a Systems?
Because of absorption
capacity of silica gel,
acid formation takes
place. The POE oil used
in R134a systems is sensitive
to this. Hence it is
not recommended to use
silica gel in R134a systems.
Q8 Can we use XH-7 on
XH-9 dehydrator for HC
blend?
Use of XH7 or XH9 for
HCs would be OK. However
XH5 which is used for
R12 is good enough for
HCs. XH7 was specially
developed for 134a as
XH5 was found to be:
a) Chemically incompatible
with 134a
b) Did not have adequate
moisture absorption capacity
c) Did not have adequate
bead crush strength
d) Inadequate resistance
to attrition caused due
to refrigerant flow.
XH9 was developed for
use with HFC152a and its
blends but was also found
suitable for a variety
of refrigerants like R22,
R134a etc.
Both
XH7 & XH9 can
be used with R12 and HCs
also but it is clearly
a case of “Overkill” since
XH5 that is used with R12
can be very well used.
b. Hydrocarbon
Refrigerants
Q1 Why CFC domestic refrigerators
of 375 grams charge and
above of R12 should not
be retrofitted with HC
blends?
The LFL is 35grams/cu
m for HC refrigerant.
Assuming a factor of
safety of 4, this figure
is further reduced to
8 grams/cu m of given
space. In a typical room
in an Indian home, of
3 X 3 X 2.5 m as shown
in the example in the
manual, the maximum permissible
HC present can be 8 X
3 X 3 X 2.5 = 180 grams
of HCs. A refrigerant
charge of about 450 grams
R12 translates into 180
grams of equivalent HC
blend charge. However
this will hold good if
the entire HC charge
of 180 grams were to
be uniformly dispersed
in the room. This never
happens in practice as
HC is heavier and stratifies
in the room, leading
to the possibility of
reaching the LFL level
at some strata. To be
still safer therefore
and considering the possibility
of even smaller rooms,
the upper limit has been
kept at 375 grams of
CFC for Domestic refrigerators.
Q2 Can we use HC blend
in Air conditioners of
capacity less than I
TR capacity?
Theoretically, using
a HC blend is like using
R12 in an AC. Apart from
the fact that the capacity
will reduce by over 40%,
if the system to be retrofitted
is a R22 system, the
electricals in the system
will have to be made
exproof or sealed, as
in the case of refrigerators
and the capillary will
also have to be changed.
The main problem again
will be the charge which
will exceed the limit
mentioned in the previous
question. Even a 0.75
TR AC has a charge of
about 600 to 700 grams
R22 and the equivalent
HC charge will be in
excess of the limits
mentioned in the previous
question. It is therefore
not recommended.
Q3 If HC blend is overcharged
how to correct it to
the actual charge?
HC blend has to be accurately
charged using weigh scales.
In the event of an accidental
overcharge, it is very
difficult to bring the
charge back to the desired
figure by purging and
checking the back pressure.
Further, purging of HC
is dangerous and not
desirable. The performance
of a system using HCs
is highly sensitive to
the charge and therefore
the only other alternative
is to vent the entire
charge to the outside
(well ventilated place)
using the recommended
method and recharging
the unit again accurately.
Q4 In case of short winding
in a refrigerator charged
with HC, is there a danger
of fire?
For any substance to catch
fire we need fuel, source
of ignition and oxygen.
In the case of short winding
in a refrigerator charged
with HC, fuel and source
of ignition is present
but oxygen is absent, hence
there is no danger of fire.
It is dangerous when there
is a leak in the system
with a source of ignition
around.
Q5 Can HC blend be replaced
with CFC-12?
Yes. But when we are aware
of the damages that the
CFC can cause and the global
community is doing so much
to phase out CFC, is it
right on our part to re-convert
an eco- friendly refrigerator
to something that will
harm our atmosphere?
Q6
Why don’t we
recover HC?
HC
Blend can be recovered
but need to have a separate
recovery and recycling
unit. Further it should
be colleted in a separate
recovery cylinder assigned
for it also while recovering
HC Blend (mixture of R290
and R600a of each 50%)
in the initial we may get
only one gas because of “zeotropic” nature
of this Blend.
HC
Blend doesn’t
have ODP and negligible
GWP, hence letting the
gas into open air don’t
make any difference in
environmental view point.
All in all quantity present
in domestic appliances
is very low and is not
economical to recover.
Q7 How do we charge HC
blend by pressure method?
Without
any clue, charging by
reading the back pressure
(suction side) must be
done of course. The back
pressure of R600a is much
lower compared with the
other gases. At 10°C
R12/ R134a/ HC mix is appx.
1.2 bar g, R600a below
0 bar g (in vacuum). Thus
performance must be optimised
by charging.
Else charge little quantity
and switch on the system
and observe for formation/feel
of frost in the evaporator.
If not, again charge little
quantity and like wise
till formation of frost
in the evaporator. However
it is time consuming process.
Q8 For HC Blend, R 290
and R 600a mixing is locally
possible?
Yes it is possible, but
need to take precautions
(because of flammable nature
of these gases), very precise
and unwavering measurements
while performing the same.
If
though possible, it doesn’t
mean that this is legal.
For cleaning
and mixing of gases the
enterprise doing so must
have a license. Mixing
directly into a refrigeration
system is not practical.
Q9 Whether HC Blend can
be used for retrofitting
in place of R134a?
Yes, it can be used; the
capillary may need some
correction and electrical
components will have to
be changed to the non sparking
type. It may be also worthwhile
changing from POE oil (which
is highly hygroscopic and
creates problems in 134a
systems) to Mineral oil.
This would mean removing
the oil from the compressor
and flushing the system
of all POE oil and then
refilling with Mineral
oil. There is a possibility
that the Motor of the compressor
may get overloaded with
retrofit (just as it does
when R12 is filled in a
134a system) and will depend
on the rating of the original
motor.
Q10 If HC blend is charged
excess, can we remove it
in liquid stage from double
mouth drier?
HC Blends are Zeotropes
and have a fairly pronounced
temperature glide. That
is why the blend should
be charged as a liquid.
For the same reason, any
leak in the system, particularly
at a site where the gas
is part liquid and part
vapour (like the evaporator)
can cause the gas left
inside the system to change
its composition. Now, the
situation of charging excess
gas will arise only if
the gas has not been charged
by weight or if gas higher
in weight than the recommended
quantity has been charged
through pure oversight
or negligence. Whilst the
former method of charging
by traditional methods
other than weight is not
recommended for HCs (because
of the very low weight
of the charge and the extent
to which performance gets
affected even due to a
small deviation in the
recommended charge) the
latter cannot be condoned
and therefore on both these
grounds this question itself
should not be encouraged
or entertained.
On purely hypothetical
grounds, yes, the charge
weight can be reduced by
withdrawing the gas as
a liquid from those sites
where the gas exists as
a liquid. But the question
here is how will one know
how much weight has been
pulled out and how much
is left behind in the system?
One partial answer to this
is that the gas that has
been withdrawn can be recovered
into a pre weighed empty
cylinder. But this too
will not enable us to know
how much weight of the
charge is left behind in
the system and could result
in an under or overcharge
resulting in poor performance.
It can therefore be seen
that this question cannot
be entertained on any grounds
as analysed above and can
be perceived as one having
the same mindset and approach
that he still has for R12.
Q11
HC blend– What
is the flammability?
To get ignited, the concentration
of HC blend in air has
to be between the Lower
and Upper flammability
level. For HC the lower
flammability level is 2%
and Upper flammability
level is 10%. Both the
values are on Volume basis.
App. gram value of HC
for a 2% concentration
by volume is 40 gram of
HC per m3 of air, for a
10% concentration it is
200 grams per m3 of air;
pressure 1 bar.
Q12 Can HC be used in
deep freezers?
Yes it can be used however
for safety reasons it is
not advisable to use it
for appliances where the
HC charge will be more
than 150 grams.
Q13 By charging refrigerant
as liquid will the compressor
be damaged?
Yes! No liquid may enter
the compressor on the suction
side!
There are two things which
assist the evaporation
of the liquid into a vapour,
these being the Polyamide
Capillary hose (or even
Copper capillary used by
Godrej) provided by Refco
between the HC can and
the manifold and secondly
the presence of deep vacuum
in the system that convert
the liquid into a vapour.
Apart from this the throttling
at the valves for controlled
entry of the refrigerant
into the system also assists
this.
The danger of liquid entering
the compressor is the possibility
of the valve reeds breaking
or the connecting rod getting
bent or even damage to
the valve plate.
Q14 If compressor winding
in a HC blend charged system
is short will there is
an explosion in the compressor?
Three components are needed
simultaneously for causing
fire i.e. Oxygen, an ignition
source with sufficient
energy and right concentration
of HC gas. Since there
would not be any chances
for air to intrude into
compressor, chances of
fire are unlikely.
Q15 With HC if there is
a system leak will there
be fire?
If a leak takes place
in the evaporator of a
refrigerator then it can
be seen that there is every
possibility of a hazard
as the three essentials
for a fire i.e. gas (due
to leakage), air (exists
inside the refrigerator)
and a spark (from thermostat
contacts, floor switch
and lamp holder) are all
available. That is why
these components are replaced
by sealed or non explosive
components. Like wise leaks
near the compressor can
create an explosive situation
if there are sparking components
like relays and overloads
which have to be replaced
by PTCs and sealed OLPs.
Q16 Does frostbite happens
with HC refrigerant like
R12 and R22 refrigerants?
The gases which are being
used as refrigerants have
a very low boiling point
will cause frostbite when
fallen on skin and the
same case with HC refrigerant
as well.
Q17 Why do we charge HC
blend slowly?
Since the refrigerant
is charged into the process
tube of the compressor,
any liquid present must
be evaporated before it
enters the compressor,
otherwise it may lead to
compressor failure. Hence
it is advised to charge
the HC blend slowly.
Q18 Is it possible to
replace R-600a compressor
with R-134a/HC compressor?
It is possible to replace
but has to take care of
capillary, filter driers,
quantity of charge required,
Oil to be changed (but
generally comes with the
compressor) etc.
c.HFC
Refrigerants
Q1 Can we charge R12 in
a 134a system? What will
be the consequence?
Apart from violating
the Ozone Rules, the
following technical problems
can also arise:
a) Cross contamination
of R12 and 134a can lead
to an unpredictable performance.
b) Capillary for 134a
systems is usually about
40% to 60% longer than
those for R12 for the
same bore of capillary.
This will affect performance.
c) Compressor motor can
get overloaded and burn
out.
Q2 Can we charge 134a
(being a single fluid)
observing the back pressure?
Theoretically yes, if
the back pressures that
are to be obtained for
various evaporator temperatures
at different ambient temperatures,
are available from the
OEM. Here again, when charging
is done in the field, ambient
temperatures are never
constant (unlike the temperature
controlled test room of
an OEM) and a certain inaccuracy
is inherent. Considering
however, that in India,
such information from OEMs
is not available and also
considering the inherent
inaccuracy in the method,
this is not recommended
and the best practice is
to use a charging still
or even better a weigh
scale. Please remember
that compared to R12, 134a
is more charge sensitive.
Q3 How to check the pumping
of a 134a Compressor?
The best thing is to
enquire the compressor
manufacturer or OEM the
way this can be tested.
In India, KCL, Tecumseh
and Godrej have their
own recommendations.
One universal method
that can be adopted,
subject to Compressor
manufacturers agreeing,
is to use a Compressor
tester, which comprises
of a Receiver like vessel
with a relief valve and
pressure gauge at one
end and a hose with a
quick coupler at the
other end. The compressor
has to be connected to
Nitrogen through a syringe
to avoid moisture. The
syringe needle has to
penetrate the rubber
plug on the suction tube
stub. The discharge tube
stub is then connected
to the quick coupler
mentioned above. Nitrogen
pressure should not exceed
0.5 to 1 barg. After
all the connections are
made the compressor has
to build its own pressure
of 16 bar. After the
compressor is switched
off, a pressure of 12
to 14 bar must be held
for 60 seconds. The loss
of pressure should not
exceed 2 bar in 60 seconds.
Q4 Why is the Capillary
length of R134a more
than one using R12?
Capillary length for
a particular bore is
dependent on the condensing
and evaporating pressures
and the mass flow and
the transportation properties
of the refrigerants.
In this case the condensing
pressure for 134a is
about 10 to 15% higher
than that for R12 whilst
the evaporating pressures
are lower than that for
R12. The mass flow of
134a is lower than that
for R12 while properties
like viscosity etc are
different. All these
reasons lead to the capillary
length for 134a being
higher than that for
R12.
Q5 What is the viscosity
of POE oil?
POE oils have viscosities
close to that of mineral
oils that they have replaced
for HFC refrigerants.
They are graded according
to ISO standards Viscosity
grades. For refrigerators
the Viscosity for R12
is VG 32 which is similar
for POEs. However, POEs
with a little lower viscosity
VG22 is also used. Ultimately,
you should use the oil
recommended by the Compressor
manufacturer and not
any other oil as compressor
manufacturers have done
a lot of studies and
application engineering
work jointly with the
oil manufacturers in
arriving at the grade
of oil most suitable
for HFC refrigerants
for their compressors.
Q6 How long can POE oil
be kept exposed during
servicing?
As short a time as possible,
not exceeding 5 minutes
preferably. A method
that could be tried is
to use a hand pump that
has an adaptor that fits
the can of the oil and
from which a measured
quantity of oil can be
pumped into the compressor.
This will prevent exposure
of the oil to the atmosphere.
Q7 What should be the
charge weight of 134a
against a specific charge
weight of R12?
It should be approx 90%
of the charge weight
of R12.
Q8 If the evaporator
is found leaking in a
134a system, how do we
service it?
If the evaporator of
a refrigerator is damaged
and if it an aluminum
evaporator , it would
be better to replace
the evaporator and also
the compressor, as a
low side leak would have
definitely allowed a
lot of outside air and
humidity to enter the
system and contaminate
it.
Q9 During HFC charging
we are using weight as
the measure for charging
and perfectly agree that
this is better than using
suction pressure or temperature
as the basis for charging.
However, if the discharge
pressure (pumping) of the
compressor is less that
adequate, can we still
get the appropriate refrigeration
effect by using weight
as charging measure?
Charging
by weight is the correct
procedure as
long as the weight is the
one that is recommended
by the appliance manufacturer.
The manufacturer arrived
at the correct weight by
carefully optimising the
charge to the appliance’s
components. You just can’t
put any approximate weight
that you like. If after
charging according to the
manufacturer’s specifications
(normally the weight is
recorded on the nameplate
of the appliance), it is
found that the discharge
pressure is little lower
than what you normally
get by other approximate
methods and if you still
get the expected cooling
of the appliance, then
there is nothing wrong.
In case no proper cooling
takes place, the discharge
pressure is considerable
lower than expected, the
other components in the
system are ok, then the
compressor must be repaired
or replaced. There is no
cure to it with playing
of the charge. This is
of course subject to the
condition that the technician
has kept the size of evaporator,
condenser and capillary
and also compressor identical
to the one supplied by
the manufacturer.
Q10 Can anti-choke be
used in systems with HFC-134a?
No.
The POE – 134a
combination is not tolerant
to contaminants and there
will be sludge formation
in the capillary and other
parts of the system leading
to system failure.
Q11 When 134a is charged
in to a system where mineral
oil is used as compressor
lubricant, it works. How
come?
As long as there is enough
lubricating oil in the
compressor it will keep
working. Since mineral
oil is not miscible with
134a refrigerant, any oil
that will get pumped in
to the evaporator cannot
get back to the compressor
and will lead to compressor
failure in the long run.
Q12 Under what circumstances
can a flammable mixture
of HFC134a could get formed
in a workshop?
The condition at which
HFC 134a could become flammable
is as follows:
60% HFC in the air at 0.4
bar gauge pressure and
at a temperature of 177° C.
The chance for all these
parameters to match at
a time is unlikely. This
can probably happen if
there is a fire due to
other reasons in a workshop
(temperatures can reach
or exceed 177°C) and
134a gas has leaked extensively
in the workshop. At ambient
temperatures, all concentrations
of 134a in air are non-flammable
at pressures below 15psig
i.e. 2 Barg, according
to DuPont’s literature
on 134a.
Q13 What is the chemical
name for HFC 134a?
Chemical name: 1,1,1,2-tetrafluoroethane
Chemical formula: CH2FCF3
Q14 How is oil affected
by moisture?
Oil, particularly POE
oils used with HFC refrigerants
is highly hygroscopic and
dissolves a large amount
of water. This water reacts
with the POE oil to form
Polyol and Acid which are
the original building blocks
for making POE oil. The
acid in turn starts corrosion
of the system components.
The moisture also forms
sludge with the oil which
causes partial/full choking
of the capillary.
Q15
If there are leaks
in R-134a – refrigeration
system does the compressor
need to be replaced?
The practice followed
by Whirlpool, is to replace
the compressor itself if
it happens to be a leak
on the low side. However
if it is a leak elsewhere,
the compressor is not replaced.
This makes sense as a leak
on the low side can draw
in outside humid air in
big quantities and contaminate
the POE oil badly.
Q16 Will R-134a be replaced
eventually?
As
far as the Montreal Protocol
goes 134a has
zero ODP and therefore
well accepted as a CFC
replacement and hence no
question of a phase out.
As far as the Kyoto Protocol
(KP) goes, HFCs is one
of the basket of six gases
identified for controlled
emission. The KP also does
not talk of a phase out
but of emission control
because of the relatively
high GWP of HFCs.. individual
countries (particularly
in Europe) have taken their
own decisions to minimise
the use of HFCs to reduce
the risk of Global warming.
The US (which has still
not ratified the KP) is
still betting on HFCs by
tightening the emissions
and improving the energy
efficiency of HFC using
machines. As of now, therefore,
with the world’s
big power blocs thinking
in opposite directions,
there does not seem to
be any immediate threat
of a phase out of HFCs.
Q17 How to recharge oil
in R-134a system?
The
oil should not be exposed
to the atmosphere
and the best way of charging
oil is by fitting a hand
operated pump directly
on the mouth of the oil
can and connecting its
outlet through a hose to
the compressor’s
process tube whereby everything
is a closed circuit without
exposure to the atmosphere.
Alternatively, after evacuation
and leak testing, the oil
from the sealed tin can
be drawn in by the vacuum
into the compressor.
Q18
Skin condenser – how
to add 10% to it?
As we recommend while
retrofitting with 134a
a bigger condenser is required
to keep the discharge pressure
down. At the same time
we also say that we do
not recommend a retrofit
with 134a.
Q19 Can we retrofit a
CFC appliance with R-134a
by changing the oil alone?
We have to ensure that
the percentage of mineral
oil left behind should
be only 1% (at least 5%)
by weight. This is done
by emptying the mineral
oil from the compressor,
filling POE oil and then
running the system on R12
for at least 48 hours.
After that the percentage
of mineral oil is measured
using a Refractometer and
if it is found higher than
5% the process is repeated
again and again till the
percentage is brought down
to at least 5% or better
still 1%. It has been found
that it is necessary to
run the system at least
three times like this i.e.
totally for 6 to 7 days
to reduce the residual
mineral oil to this level.
All this is time consuming,
labour intensive and also
does not guarantee safe
working with 134a later.
So, even small hermetic
appliances were never retrofitted
with 134a. They were either
replaced or continued to
operate with CFCs on recovered
CFCs.
Q20 How to test the pumping
effectiveness of R-134a
compressor?
Connect the Nitrogen cylinder
to the process tube of
hermetic compressor using
a two stage pressure regulator.
The discharge side of the
compressor to be connected
to the receiver or a condenser
coil having appropriate
capacity. The other end
of the receiver/condenser
coil to a pressure gauge
which can read 0 to 300
PSIG.
Check for leaks at all
joints using soap solution
and then supply Nitrogen
gas at a constant pressure
of 20 PSIG in the process
tube of the compressor.
Start the compressor and
run for few seconds to
build a head pressure of
value as specified in the
table below. On attaining
the specified discharge
pressure stop the compressor
and check for drop in pressure
for a period of one minute
and verify whether it falls
with in the specified limit
in the table. If the pressure
drop exceeds the specified
limit, the compressor has
a pumping defect, otherwise
the compressor is OK.
Group Leak rate per MIN
(PSIG) Head pressure (PSIG)
AE 30 125
AJ-CAJ 30 125
AH/CR 6 40/45 150
AG 60 200
Q21 How a chocked R-134a
system will be checked
through suction side?
A partial chock will result
in a very low suction pressure
(even a deep vacuum) and
higher than normal discharge
pressure.
Q22 Is it required to
change expansion valve
and other components for
CFC 12 system while retrofit
with R-134a?
In thermal evacuation
systems, the expansion
valve has to be changed
or reset to adjust to the
higher pressure ratio.
Other components like filter
drier, compressor oil,
capillary length etc also
have to be changed.
Q23 Capillary size design
of R-134a system while
retrofitting R12 system?
The capillary tube is
usually 10-20 % longer
for R-134a systems.
d. Recovery & Recycling
Q1
Can we use a common
Recovery machine
for both
CFC & HFC systems?
A common recovery machine
can be used, if every
time, a change in refrigerant
handling is encountered,
the machine is evacuated
and all traces of the
earlier handled refrigerant
is removed. A vacuum
of at least 1000 microns
is needed for this. However,
as such disciplined procedures
are seldom practiced
in the field, it is safer
to use separate Recovery
machines for each of
the refrigerants. Separate
Recovery cylinders are
to be used for each refrigerant.
It should be remembered
that R12 & 134a form
a high pressure azeotrope
in all proportions and
a contamination exceeding
2 to 3% is bad.
Q2 Any simple test to
identify the acidity
in lubricants?
The simplest test is
to use a litmus paper
that turns from blue
to red. This only tells
you of the presence of
acid but not whether
it is at an acceptable
level or not. A better
test is the use of 'Acidity
Test Kits' which are
not made in India but
available through Total
Line of Carrier Aircon.
This is made by Sporlan
of the USA and comprises
of 3 bottles: A small
bottle with a colourless
liquid for Mineral oils,
another small bottle
with a colourless liquid
for POE oils and one
large bottle with a orange
coloured solution. The
procedure is that the
colourless liquid from
one of the small bottles
(depending on which oil
is being tested) is poured
into the big bottle containing
the orange coloured solution.
This will turn the colour
orange to Purple. Add
the sample oil to the
large bottle and shake
15 times. Observe the
colour after this:
• If it is still purple,
it is ok and not acidic.
• If the colour turns Orange,
it is somewhat acidic
and not very satisfactory.
For POE, it indicates
0.17 to 0.23 TAN.
•
If the colour turns yellow,
it is unsatisfactory
and to be rejected. For
POE, it means a TAN>0.23
For low temperature hermetic
applications like refrigerators
TAN lower than 0.17 is
preferable. However refrigerant
(oil) that indicates Orange
colour can be used for
Auto AC. TAN stands for
'Total Acid Number' and
indicates the weight of
KOH (Potassium Hydroxide)
in mg required to neutralise
a gram of liquid containing
the acid.
The price of such a kit
(for a one time use) is
approx Rs 500.
Q3 What could be done
with the recovered and
stored CFC?
This is a difficult to
answer at this stage as
there are no rules or regulations
existing in the country.
Yes recovered refrigerant
can be reused, preferably
in the same system from
which it was recovered
as long there is no Motor
burnout. However if facilities
are available to do a quick
moisture or acid test of
the refrigerant, the refrigerant
can be used after recycling
depending on the results
of the test. Even here,
it is better if the recovered
refrigerant is used in
the same system from which
it was recovered, in the
absence of any rules or
regulations. The problem
is the non availability
and high costs of recycling
machines. However NCCoPP
is working towards formulating
country guidelines for
Recovery and recycling,
proposals are under way.
Q4 : What to do with the
recovered refrigerant?
(Category 4)
Recovered refrigerant
when not contaminated or
only marginal can be used
in the system again after
repair. (With a compressor
burn out, refrigerants
are heavily contaminated.)
Of course, best is to recycle
all refrigerant before
reuse. But this is an economic
question as multi pass
recycling machines are
not cheap and thus only
economical if sufficient
refrigerant can be recycled
over time. For this a group
of technicians from the
same locality could join
together and purchase one
machine and start recycling.
Refrigerant recycling and
reuse can only be done
if refrigerants are not
mixed! Hence keep separate
cylinders for each and
every recovered refrigerant.
In the future the Govt.
might start some recycling
centres at some selected
cities or towns and technicians
will be able to make use
of the same.
Q5 How will have to keep
recovered refrigerant?
CFCs and HFCs are recovered
in a recovery cylinder
using a recovery machine.
It is also recommended
that the cylinder be labelled
with the following information:
• Name of the refrigerant
stored inside
• Weight
For further details please
refer HIDECOR MSE Handout.
e. Servicing
Practices
Q1 Using Nitrogen at 10bar
makes the oil in the condenser
and evaporator to come
out?
Flushing need be done
at 5 bar only.
Q2 How do you read microns
in the Refco Vacuum Gauge?
The Refco Vacuum gauge
is calibrated in Milli
bars or mb and the smallest
or lowest reading that
can be read is 10 mille
bars which is about 7600
microns. For reading
in microns below this,
it is necessary to use
a gauge that can read
lower than this i.e.
Pirani or Thermo couple
gauges.
Q3 Trichloroethylene
also contains Chlorine
and is recommended for
cleaning. Will it not
also contribute to the
Ozone layer damage?
The chlorine in Trichloroethylene
does not rise to the
stratosphere and contribute
to ozone damage. It is
not as stable as CFCs
and the chlorine in it
gets separated and lost
in the lower atmosphere.
It is therefore not listed
amongst the ODS in the
Montreal Protocol that
needs to be phased out.
Q4 What is the correct
measure of Vacuum, is
it the level of vacuum
or the time the Vacuum
pump is kept running?
The level of Vacuum,
as measured in microns
of Hg in a Vacuum gauge
(that is of the Pirani
or Thermocouple type)
is the right measure
of Vacuum. The recommended
is at least 200 microns
(100 microns desirable)
Hg for 134a and 500 microns
Hg at least for R12.
After achieving this
level of Vacuum, the
Vacuum pump should be
isolated with the valve
and stopped and the Vacuum
holding capacity of the
system should be checked.
If the pressure rises
slowly and then stabilises
at a higher level of
microns, it means that
there is some moisture
still remaining and the
Vacuum pump should be
restarted and reconnected
and run again for about
10 minutes and the rise
in pressure checked again
and this process should
be repeated till the
rise in pressure is as
low as possible, suggesting
that almost all the water
vapour has been removed.
After this has been achieved,
the Vacuum pump should
be run for another 5
to 10 minutes before
proceeding to the next
step of charging refrigerant.
Q5 Evacuation needed
for HFC is to be as low
as 100 Microns. Is such
low levels needed for
HCs also?
HCs can be evacuated
to the same levels as
CFCs i.e. at least 500
Microns. Moisture can
be as detrimental in
an HC system as in a
R12 system. Further the
solubility of HCs in
oil as well as the solubility
of moisture in HCs is
higher than in the case
of CFCs. Therefore it
is better to evacuate
HC systems to at least
500 microns and for HFC
system is at least 200
microns.
Q6 The ideal clearances
between tubes, for brazing,
for good capillary action
has been mentioned as
0.05mm to 0.200mm. What
should be the depth of
insertion?
The depth of insertion
gets automatically determined
when a correct swaging
tool is used to swage
the end of a tube which
is to be brazed to another
of the same size. It
is usually kept equivalent
to the OD of the tube.
It is possible to also
braze a smaller tube
of 1/4" to a bigger
tube of 3/8" tube
without any swaging.
However the clearance
between the tubes becomes
much higher than the
permissible 0.200 mm
and here the insertion
has to be longer (about
0.75 to 1 inch) and a
brazing rod with 15%
Ag and 5% P has to be
used even for Cu to Cu
brazing. However when
brazing a 3/16" Cu
tube to a 1/4" Cu
tube it will be necessary
to swage the end of the
1/4" tube, as otherwise,
the clearance between
the tubes becomes too
small (0.025mm).
Q7 What is the purpose
of using flux? What is
it made of?
Oxidised metal surfaces
cannot be brazed and
thus need cleaning beforehand.
This cleaning action
is performed by the Flux.
Flux reacts chemically
with the metal oxides
and dissolves them and
prevents oxides from
reforming. Flux becomes
fluid at brazing temperatures
and adheres to the base
metal. Flux is then displaced
by the molten filler
in the brazing process.
Flux is required when
brazing ferrous metals
with filler rods not
containing Phosphorous.
Fluxes are formulated
from many chemicals e.g.
acid, Borates, Fluorides,
Fluoborates, Deoxidizes,
water & wetting agents
and are available in
the form of powder, paste
and liquid.
Q8 What is the minimum
required level of Ag content
in Brazing rods?
Cu to Cu brazing does
not need Ag though the
presence of 2% Ag helps
a lot. However 15% Ag rods
is recommended even for
Cu to Cu brazing where
the clearances between
the tubes is high , as
explained under Question
no 6 above. For Cu to steel
or brass, at least 35%
Ag is needed, Infact, 45%
Ag would be the best.
Q9 Whether it was possible
to use Dry Ice (solid CO2)
in a cold trap to eliminate
the moisture that was being
removed from the system?
Yes, this can be done,
as it will help in reducing
the load on the Vacuum
Pump. An article on how
to use the Cold trap
with Dry Ice is attached.
Q10 Availability of portable
Nitrogen and Oxygen cylinders?
At present only Godrej
have succeeded in developing
sources for small Nitrogen
and Oxygen cylinders
in Mumbai. It has to
be seen whether the suppliers
have an all India (or
at least in HIDECOR focus
areas) distribution network
and a study will have
to be done on this.
Q11 Cost of sealed electrical
components when retrofitting
to HCs?
Sealed door switch - Rs.
07.25/-
Sealed lamp holder – Rs.
10.60/-
Sealed OLP for HC compressor – Rs.
32.00/-
PTCR for HC compressor – Rs.
35.00/-
Sealed thermostat – Rs.
95.00/-
Note that all the mentioned
costs may vary from place
to place
Q12 How do you know what
gas is inside a system
if the label on the refrigerator
is missing?
Keep the refrigerator
in a well-ventilated area.
Connect a piercing valve
to the process tube of
the refrigerator compressor
and at the outlet of the
piercing valve connect
a long capillary. Open
the piercing valve slowly
and allow small quantity
of refrigerant to come
out on to a match/ cigarette
lighter flame.
R134a when burned, the
colour of the flame does
not change.
R12 when burned, the outer
lining of the flame gets
a greenish tint.
HC (R290/R600a) burns
by itself.
HC
(R600a) burns by itself.
But pressure in the systems
is much lower (at 30 °C
appx. 2.5 bar gage) than
with the other gases (at
30 °C appx. 6.5 bar
gage). Hence a pressure
test will indicate immediately
whether it is R600a or
another gas. But no R600a
is on the market in India
at present.
Such tests should be done
very carefully trough a
capillary and in open air.
Burning of R134a and R12
produce toxic gases. HC
is flammable.
Question is harder to answer
when no gas is in the system
anymore. The label on the
compressor might tell,
sometimes this is also
engraved in housing. The
age of a refrigerator is
also a telltale. Also,
the name of the fridge
may tell. If the name indicates
environmental friendly
then it is R134a or HC.
There might be an indication
of the manufacturer and
type of the fridge and
the easiest way to find
out is thus to call the
service line of the manufacturer.
If the fridge is so old
that they donot know anymore,
then it is R12 anyway.
All fridges before 1996
are most probably R12.
Maybe there is a manual
still with the owner? The
filter dryer used might
also indicate (type XH7 & XH9
used for R134a, type XH5
used for R12 & HC systems
and XH6 or XH9 used for
R22)
Charging:
Without any clue, charging
by reading
the back pressure (suction
side) must be done of course.
The backpressure of R600a
is much lower compared
with the other gases. At
-10 °C R12/ R134a/
HC mix is appx. 1.2 bar
g, R600a below 0 bar g
(in vacuum). Thus performance
must be optimised by charging.
Q13 Why do compressors
pump oil? / How does the
system get choked with
oil?
In any system when a compressor
is working, certain amount
of lubricating oil is always
pumped out of the compressor
along with the refrigerant,
however this returns to
the compressor along with
the refrigerant because
of its miscibility with
the refrigerant. In the
evaporator, oil viscosity
is high due to the low
temperatures there. If
the refrigerant mass flow
gets reduced due to partial
capillary choke or partial
gas leak the refrigerant
velocity will not be adequate
to carry the oil with it
back to the compressor.
This results in system
oil choke.
Q14 What is the harm in
using locally re-winded
compressor with R 134a?
It is not recommended
mainly because the insulating
material used by the local
re-winders may not be compatible
with R134a and POE oil
used in R134a system.
Q15 How system heating
is affected for getting
vacuum?
Firstly heating the system
is not recommended. This
may damage electrical components,
quality/sensitivity of
oil may get affected and
later this may lead to
system failure.
Q16 What is the effect
of using anti-moist in
a system?
Anti-moist
is a contaminant. The
POE – 134a combination
is not tolerant to contaminants
and there will be sludge
formation in the capillary
and other parts of the
system leading to system
failure. The same effect
could be expected in other
refrigeration systems;
hence it is not advisable
to use anti-moist.
Q17 How can oil be identified
in a compressor with unknown
refrigerant?
Without tests to be done
in a laboratory this is
difficult. Hence for a
technician first find out
what has was/is in the
system. This issue is covered
earlier on. If it is observed
to be HFC refrigerant for
sure the oil in the compressor
must be POE oil, else if
it is CFC then the oil
should be mineral oil.
Apart from the above if
it is HC Blend then the
oil could be either POE
or mineral oil, but most
likely the later.
Q18 Importance of vacuum
in microns
Micron is the smallest
unit for pressure measurement.
For example 1 mm of Hg
is equal to 1000 microns
(1000 times smaller) ,
while evacuating the domestic
refrigeration system pressure
may come down to around
500 microns Hg. Hence for
accurate measurement it
is necessary to measure
the pressure (vacuum) in
microns.
Q19 Why oil is not coming
out of compressor during
deep vacuum?
The compressor oil has
certain density and boiling
point. The vacuum levels
(down to 200 microns) reached
normally is well above
the vapour pressure of
oil in the compressor.
Hence oil will not evaporate.
Also the refrigerant In
and Outlet of compressor
side are well above the
oil level- hence there
is no chance/possibility
of sucking out the oil
from compressor.
Q20 Why dry nitrogen should
be used?
Nitrogen
is an inert gas and therefore
will not
react with the compressor
oil as Oxygen (which is
present in air) would.
The dry Nitrogen would
have a purity of 99.997%
and a dew point of at least
-40°C. Therefore the
Compressor oil is unaffected
and the moisture present
in the system will get
absorbed by the dry Nitrogen.
Q21 Can halide torch
be used to check leaks
of HC and HFC?
The answer is NO.
a) HFC refrigerants decompose
to form toxic products
when heated.
b) As HC gases are flammable,
Halide torches are not
recommended for leak detection.
Since the gas in the system
is not under safety conditions/a
controlled burning.
Q22 What are the standing
pressures of HFC 134a and
HC Blend?
At
30 °C
HFC 134a: 98.26 psig
HC blend: 82.37 psig
Q23 Do the PTC replay
work on all capacity compressors?
HIDECOR recommends PTCs
in place of relays to prevent
sparking when using HCs.
PTC relay does work with
all capacity compressors
and is recommended for
systems using HC Blend.
Larger capacity compressors
(which use more than 150g
of HC Blend in domestic
appliances, the same for
250 g in commercial appliances)
are not recommended for
using HC Blend and the
same valid for PTC relay.
Positive Temperature Coefficient
(PTC) relays are solid
state devices which are
to be used in systems handling
flammable refrigerants
like HC blends. This option
will make the compressor
safe to work with HC refrigerant.
Q24
Chlorine – what
is the atomic weight?
The Atomic weight of chlorine
is 35.5.
Q25
Bar-kg conversion – pressure?
1 bar = 1.0197 kg / sq.cm.
Q26 Why use 2% silver
rod when brazing?
The
addition of Silver firstly
reduces the temperature
at which the alloy starts
melting. The Solidus will
be at 643°C against
710°C where there is
no Silver at all. This
means less heat and therefore
less heating of the system
components. Secondly the
melting range increases
from 643°C to 788°C
as against 710°C to
794°C where there is
no Silver.
The advantage here is
that the flow of the
melting alloy is slower
than what it is when
there is no Silver. This
helps in filling gaps
by working on the molten
alloy than depending
purely on capillary action.
This helps when soft
annealed copper tubes
are used as in the case
of small appliances like
refrigerators and freezers
using hermetic compressors
as the clearances of
the brazing joints are
never uniform. On the
other hand, the use of
Alloys without Silver
results in a fast flow
of the molten alloy over
a narrower temperature
range and the filling
of the joints is dependent
entirely on capillary
action for which the
clearances have to be
correct and uniform.
Therefore a better joint
is possible with 2% Silver
rods. As the silver content
increases and reaches
15%, the melting range
increases and the flow
rate becomes even slower
and this would be good
for filling uneven clearances
and creating fillets.
All what has been stated
above is for copper to
copper brazing and all
the alloy rods referred
above contain Phosporus
from 7 to 5% which acts
like a flux.
Q27 What is 100% vacuum?
A perfect vacuum is a
condition that does not
exist. High-vacuum coating
chambers pump down from
an atmospheric pressure
of 760 Torr to a pressure
of 1 x 10-5 Torr. This
means that for every 100,000,000
molecules of air in the
chamber before pump down,
only about 1 remains after.
However for Refrigeration
purposes it is normally
not possible to reach a
system vacuum lower than
250 microns or 0.025 mm
i.e. 0.025 torr.
Q28 Will oil boil at deep
vacuum?
Mineral oils boil at approximately
250 microns, after pump
for days only boil out
a teaspoonful or less.
Q29 Will R-134a / HC affect
the material used as Evaporator
i.e. Aluminium?
The material used in the
manufacture of Evaporator
i.e. aluminium can suit
to HFCs and HCs. This situation
would be critical when
moisture enters in R-134a
system, which results in
acid formation and eventually
eat away the Aluminium.
Hence it is recommended
to evacuate the system
properly.
Critical with R-134a is
acid formation if moisture
enters system and acid
can eat away AL then. Hence
one more good reason to
evacuate properly.
Q30 How to clear the brazing
flux in the compressor
discharge line?
Need to reopen the joint
and replace with new discharge
line/cut off previously
brazed portion. If there
is no passage block inside,
then presumed to be everything
is OK.
Q31 How do we differentiate
between R12 and R22?
R12
gas will indicate a standing
pressure of
93.93 PSI R22 gas will
indicate a standing pressure
of 180 PSI at 30°C
in a cylinder.
Q32 Why a single stage
vacuum pump is not enough
to draw a vacuum of 500
microns?
Single
stage vacuum pumps can’t
draw low vacuum on account
of inherent
oil contamination and lower
compression ratios.
Q33 What is the substitute
gas for R22?
R417A is one of the replacement
for R22 as it has zero
ODP and suitable for new
equipment and as a drop-in
replacement for existing
systems. Some other refrigerants
under consideration are
R-407C (drop in substitute),
R410-A (changing compressor
as pressures are higher)
and R-290 (Pure Propane).
Source: The Comfort Environment
Group Limited, Comfort
Works, Newchapel Road,
Lingfield, Surrey RH7 6LE
(UK).
Q34 What is PTC replay?
Positive Temperature Coefficient
(PTC) relays are solid
state devices which are
to be used in systems handling
flammable refrigerants
like HC blends. This option
will make the compressor
safe to work with HC refrigerant.
Q35 Which chemical is
to be used for cleaning?
For
cleaning we can use trichloro
ethylene, don’t
use CTC as it is ODP substance
and is controlled under
Montréal protocol.
However after cleaning
the trichloro ethylene
should be completely evaporated.
Q36 Which are the oils
used in vacuum pump?
The oils with very low
vapour pressure and will
have no degassing effect.
3. Ozone Depletion and
environmental impact
Q1 Why do Green house
gases allow light (heat)
rays/waves in one direction
only from the earth to
the sun?
The solar radiation coming
from the sun and passing
through the green house
gases have shorter wave
length whereas the thermal
radiation reflected from
the Earth's surface has
longer wave lengths. The
greenhouse gases trap the
reflected radiation only.
Q2 What is the mean (average)
temperature of the Earth?
The
mean temperature was
about 15°C. But the
doubling of the CO2 levels
in the atmosphere in the
last 100 years is expected
to raise temperatures by
1.5 to 5° C this century.
This can be compared with
a rise of 0.4°C in
the entire 20th century.
A one percent rise in surface
temperatures could cause
major disruptions in weather
patterns, flash floods
and unexpected droughts.
Q3 Why trichloroethylene
does not effect the Ozone
Layer?
Trichloroethylene degrade
within 6-8 days
is regarded as low
troposphere ozone creators
as well
as insignificant
(<0.5%)
contributors to acid
rain formation. The ODP
(stratospheric Ozone
Depletion Potential)
is negligible and they
are not regulated under
Montreal Protocol.