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Daily Tips
Controlling
leakage is an important part of any lubrication program. Here is a list of
potential causes of leakage:
-
Design/Selection
- through improper selection, sizing and tolerances of elements; improper
closure of the clearance space between two mating or close running elements;
improperly selected seals; use of defective, incompatible or highly porous
material, and being unaware of what operational conditions might be imposed
on the system.
-
Manufacturing
- through inadequate control over tolerances, mating of elements, surface
finishes, material composition and foreign matter, assembly and
quality.
-
Operation
- through over-pressurization, over-loading, over-speeding, high dirt
ingression, high temperature, fluid dilution, etc.
-
Maintenance
- through ineffective maintenance practices and strategies; not recognizing
the signs of conditional failure, etc.
More
Great Tips - From the Message Boards
The
Practicing Oil Analysis Message Boards are a great place to
express your opinions, get your questions answered, share
experiences and make friends.
We've
gleaned the Message Boards for useful information and found
some great information on greases to share with you.
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Subject:
mixing incompatible greases
From:
Eric
Date:
19-Jun-00
does
anyone know what exactly happens when two incompatible
greases
are mixed in a bearing, such as a lithium 12 hydroxy
based
grease and a bentone clay based one. I know that it may
change
the viscosity of the greases, but are there any other
"side
effects" of mixing greases?
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Subject:
RE: mixing incompatible greases
From:
Rich Wurzbach
Date:
20-Jun-00
Eric,
Actually,
it doesn't change the 'viscosity', but rather the consistency
of the greases. Greases are made up of a base-oil and a
thickener. The base-oil has its own viscosity, and that is what forms
the lubricating film in the application. The thickener serves
to hold the oil in place where the lubrication is desired, and
keeps out contaminants.
When
incompatible greases are mixed, the consistency usually decreases,
making the mixture softer. This may make it less effective
at keeping the grease in the area needing lubricant. Also,
the oil may 'bleed' out of the grease in such a mixture, leaving
behind the thickener, which can harden. The hardened thickener
may prevent subsequent shots of grease from reaching the
bearing. Without the oil, the thickener is ineffective at lubricating
the bearing and lubricant starvation failure can
occur.
The
incompatibility charts are meant as a guideline. If you have mixed
incompatible greases, or are considering doing so, the best thing
to do is to mix up a batch of the two greases in the ratio anticipated
and compare qualities. ASTM cone penetrating test and dropping
point tests can be performed, or you can get a quick idea
by using a tongue depressor and comparing the stiffness of the
grease mixture to the unmixed greases. You can also put a dab of
the mixture alongside dabs of the new greases and inclining the surface
to check for excessive bleed.
Always
avoid mixing unlike greases, but if it is unavoidable, some
of these techniques may help you decide the proper course of action.
Rich
Wurzbach, Maintenance Reliability Group
DAILY TIPS
- Viscosity Index (VI) is determined from viscosities
measured
at 40 and 100
degrees C (100 and 210 degrees F). Typically, the
VI is then found from standard VI tables.
Proper baffling is an important part of hydraulic
reservoir design. Oil
residence time in a reservoir influences air and
water separation efficiency. With baffling, the oil is forced
to remain in the reservoir longer, improving water shedding
and air detrainment.
MORE
GREAT TIPS
Today
we are going to look at an excerpt from Dr. E. C. Fitch's book "Proactive
Maintenance for Mechanical Systems." This passage
is extracted from the fluid chemical stability section and
describes some of the best methods for determining oxidation
in equipment:
"Once
the oxidation process occurs, five major changes in the oil
result in the following:
-
Color
becomes darker - changes from transparent or translucent
in color to some degree of discoloration toward the
point of complete opacity.
Odor
becomes pungent and acetic due to the presence of excessive
organic petroleum acid and similar products of oxidation.
Acidity
increases - changes from a Neutralization Number from 0.06
to 0.12 KOH mg/g to well above 2.0 can occur.
Viscosity
increases - the viscosity of an oil frequently may double
or triple due to oxidation. Oxidative thickening is capable
of producing fluids that have the consistency of molasses-like
sludge under high operating temperature conditions.
Insolubles
precipitate (sludging occurs) - after an induction period,
the deterioration of an oil gradually accelerates until the
formation of organic acids or deposition of sludge completely
destroys the oil.
DAILY
TIPS
tendency
of grease to withstand water washout in bearings. A ball
bearing is rotated at 600 rpm; while 100ºF water flowing at
five cubic centimeters per second impinges on the bearing housing.
The test measures the percent of grease washed out in one
hour. The test is repeated with 175ºF water.
The
three steps of proactive maintenance are:
-
Define
the target root cause property (i.e., cleanliness level)
Achieve
the target (i.e., improved contamination control)
Monitor
(measure) the property regularly
MORE GREAT TIPS
Today
we are going continue our series of excerpts from Dr.
E. C. Fitch's book "Proactive Maintenance for Mechanical Systems."
This passage is extracted from the fluid chemical stability
section and describes some of the best methods for determining
oxidation in equipment:
"A
slight discoloration of the oil is nearly always present during
the initial stages of oxidation. This discoloration increases
as the process continues and the decoloration is accompanied
by a drop in interfacial surface tension and a rise in
viscosity, specific gravity and the neutralization number.
The
rise in viscosity and acidity are not necessarily interdependent.
"Primary
oxidation will cause a rise in acidity which will ultimately
level off, at which point the viscosity may rise at
an extremely rapid rate. Such increases in viscosity rate usually
occur due to the generation of oxidation products of high
molecular weight, held in fluid suspension. Paraffinic base
oils
are less apt to produce sludge at an earlier stage as those of
a polynapthenic base."
"The
oxidation rate and the degradation products increase not only
with increasing temperature, but also with increases in agitation
(turbulence) and contamination - air, water, metallic particles,
dirt and dust. The oxidation stability varies not only
with the viscosity grade of the oil but also with the quality
of the base stock. In addition, the actual base stock
from
which the hydraulic fluid was derived and refined also affects
the rate of oxidation."
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