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Project Name: |
Gravimetric Analysis of Filter Model 27/27 B |
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Client: |
Harvey Klassen CC Jensen/Klassen Specialty Hydraulics Inc. |
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Principal
Consultant: |
Mark Barnes, Noria Corporation |
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Date: |
25 February, 2002
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This report details the findings of a gravimetric
analysis of a CC Jensen filter sample supplied by Harvey Klassen of Klassen
Specialty Hydraulics Inc. As per
the original scope of work for this project, this report outlines the amount of
material trapped in a representative sample of the filter.
In addition, based on an ICP analysis of the filter residue, further
speculation is made as to the nature of the material trapped by the filter and
possible route causes of the problem. However,
without further detailed study of the mechanical system as a whole, and further
comprehensive testing of the oil and the filter, a definitive root cause cannot
be determined, although some inferences can be made.
Filter – Visual Inspection and ICP analysis.
A cursory visual inspection of the filter indicates
that the contaminants trapped by the filter are organic in nature, indicating
that this material is likely due to by-products of lubricant degradation.
Furthermore, by looking at the cross sectional area of the filter, it is
clear that the contamination is evenly dispersed throughout the full depth of
the filter medium indicating that the contaminants are every small and able to
penetrate into the center of the medium.
In order to gain some understanding of the type of
material trapped by the filter, the filter residue was dissolved in kerosene and
an ICP-AES measurement made. 24
elements were measured ranging from wear metals to common contaminants and oil
additive elements. Those elements
that showed significant concentrations in the ICP analysis are given below:
|
|
Si/ppm |
Fe/ppm |
Ba/ppm |
Ca/ppm |
Zn/ppm |
P/ppm |
|
Sample 1 |
46 |
44 |
72 |
1004 |
7597 |
2160 |
|
Sample 2 |
22 |
34 |
54 |
749 |
6481 |
1990 |
The absence of significant concentrations of wear
metals (e.g. iron) and contaminants (e.g. silicon) compared to the amount of
residue in the filter (see below) indicates that the material trapped in the
filter is likely a direct result of lubrication degradation.
The presence of oil additive elements (Ca, Zn and P) is not uncommon in
this type of situation. It is highly unlikely that these elements are found in the
filter as a direct result of filtration, since additives typically found in AW
hydraulic fluids such as Nuto H are dissolved in the oil and will not be
stripped directly by this type of filtration.
Their presence is likely as a direct result of breakdown of these
additives due to whatever mechanism is causing oil degradation to occur (see
below). The concentrations found in
the filter by ICP are not high enough to indicate that most of material is
anything other than organic in nature. Without
further analysis, including XRF data, the exact molecular form of these additive
by-products cannot be determined.
Filter Gravimetric Analysis
Gravimetric filter analysis was performed at
Southwest Research Institute (SWRI). The
procedure involved a reflux distillation procedure using a soxhlet apparatus, in
conjunction with hexane as the solvent. Heptane was used to remove all oil soluble and insoluble
material to be extracted from the filter sample.
A 150-mesh screen was used to prevent filter material entering the
reaction vessel and being counted as filter residue material.
After the distillation process the hexane was removed by rotary
evaporation and the amount of material left behind weighed in relation to the
mass of filter sample originally used.
| Filter sample at end of test (EOT) | |
| Residue after heptane extraction |
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Two filter samples were, each constituting a pair of
disk elements. Each sample was
broken-up and a small portion refluxed for 3 days to remove all material.
The mass of each filter sample before and after reflux was determined,
together with the mass of material left behind after evaporation of the hexane.
Data from the test procedures was as follows:
|
Sample 1 |
Initial
weight (g) |
Final
weight (g) |
Gain/Loss |
|
Soxhlet |
302.339 |
302.337 |
0.002 |
|
Flask |
293.301 |
309.557 |
16.256 |
|
Filter |
31.0139 |
15.0416 |
15.9723 |
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|
|
|
|
|
Sample 2 |
Initial
weight (g) |
Final
weight (g) |
Gain/Loss |
|
Soxhlet |
317.36 |
317.361 |
0.001 |
|
Flask |
296.642 |
313.052 |
16.410 |
|
Filter |
32.4575 |
16.2115 |
16.2460 |
Based on the gravimetric analysis study, it is clear
that each element pair held approx. 16 g of filter residue per 16 g of filter
media although it cannot be determined whether the filter is indeed saturated at
the levels measured in this study. Based
on this analysis, it is estimated that filter can hold as a minimum its own
weight in trapped contaminants and lubrication by-products.
Based on ICP data, it appears that in this instance, the overwhelming
majority of the filter residue is organic material from breakdown of base oil
molecules.
Root Cause Analysis
Based on the data available, it is our opinion that
the filter has become plugged with the by-products of oil degradation.
Oil degradation typically occurs in one of two ways, either oxidative or
thermal fauilure. However, based on information supplied by Gerry Trodd, it is
our understanding that no increase in acid number from oil samples taken from
the reservoir was observed in this instance.
This factor is consistent with a thermal failure mechanism.
Thermal failure is typically caused by one of two
mechanical issues; either contact of the oil with excessively hot machine
surfaces, or by an effect called micro-dieseling. Micro-dieseling is a common problem in hydraulic systems, and
is usually as a result of excessive air entrainment. As entrained air bubbles pass through a hydraulic pump, the
increase in pressure results in an adiabatic compression causing the temperature
to rise. This increased
temperature, which may reach several thousands °F
results in complete degradation of the oil, causing oil darkening, sludge and
varnish formation and additive mortality due to thermal reaction.
This is a particular problem with sulfurous additives such as ZDDP
antiwear additives used in AW hydraulic fluids and may explain the high Zn and P
levels found in the filter residue and the depletion of these additive elements
in bulk oil samples. The data
obtained from this study are all consistent with thermal degradation as the oil
failure mechanism.
Further confirmation may be obtained by running a
differential FTIR scan of new vs. used oil.
Typically, under conditions of thermal failure, a significant increase in
nitration by-products is observed at 1630 cm-1.
This test should be considered to further evaluate thermal failure as a
root cause.
Should thermal degradation due to air entrainment be
determined as the root cause, it is strongly recommended that the source of the
excessive air entrainment be investigated and corrected.
While ultra-fine filtration is an excellent solution to extending machine
life, it should not be considered as a long-term solution to excessive
sludge/varnish build-up and is simply removing the by-products of oil
degradation, after the problem has occurred.
Common conditions that can lead to poor air
detrainment of the oil include, excessive contamination with water and other
impurities, poor system design such as plunging return lines, poor reservoir
design and in-adequate oil residence time and suction line leaks.
It is strongly recommended that each of these factors be considered and
reviewed rather than relying on oil filtration to remove degradation
by-products. The use of a diffuser
on the return line, if not already in use, together with appropriate reservoir
baffling and a wire mesh screen should be considered.