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48 | Mar/Apr 2011 | ME | maintenance & asset management vol 26 no 2
INTRODUCTION: THE STARTING YEARS
Yallourn Power Station was initially
built in the watch of Sir John Monash,
citizen soldier (a First World War
Lieutenant-General) and engineer. It was
the biggest in the state from 1924 up to
1966. Such places tended to have the
best engineers and I was fortunate to
have two excellent bosses there. They had
responded to a request from the manager
of maintenance. He was apparently holding
a sheaf of fault reports, overtime returns
and spare parts usage reports on a turbine
that had just come back into service after
a major strip-down. ‘There has to be a
better way than this’ was his cry. Research
reported in POWER and ASME papers
led to the ‘Valves Wide Open’ test being
applied. My involvement in testing 60MW
and 120MW turbines
there gave me the topic
for my engineering course
dissertation. Performance
tests were also performed
on the boiler feed pumps
and used as a guide to
overhaul.
Measurement and
analysis of the vibration in
a machine, as a guide to
its internal condition was
then very basic. We had a
Philips velocity transducer
and a read-out box that
gave overall vibration in
thousandths of an inch. For
some machines of rotation
speed below 900 rev/
min, a multiplier of 1.5 was
used (nobody explained
why, but later I learned that
it was because velocity
transducers have a natural
frequency below about 900
c/min). We could examine
It had three 200MW units in service, but
would grow by a unit each year to reach
eight, its current size. The boilers were
essentially identical, but there were two
makes of steam turbines and boiler f eed
pumps.
The vibration measurement programme
was as at Yallourn, but more use was made
of the balancing instrument to fi nd relative
phase angles of the 1X vibration to give
a crude operation defl ection shape. For
routine monitoring of the steam turbines,
permanent numbers were painted around
the rotor line at a visible section.
Case study 1A strange vibration was experienced on
the newest machine at the generator
drive-end bearing. When run up following
a shutdown, the machine vibration was
unacceptably high. The operators tripped
it and ran for some hours on turning gear
(low speed rotation at 30 rev/min). Back on
line, the vibration was now acceptable. This
happened repeatedly: sometimes all would
be OK after a shutdown, sometimes not.
Vibration measurements with our crude
instruments on line in both states showed
that the vibration amplitude and phase
angle differed on every run! All I could
say was that ‘these symptoms indicate
that there is something loose inside the
generator rotor around that end’.
Strip-down was arranged and the generator
rotor examined closely. Nothing was found.
Eventually, a message came from the
OEM saying that one of the rotors – that
one – was non-standard. At the end of
manufacture, the rotor centres were bored
out to about 100mm diameter, and the
Lessons Learnt in 45 Years of Condition
Monitoring
Ray Beebe MSc, CEng, MIET
School of Applied Sciences and Engineering
Monash University Gippsland Campus, Australia
the output on a CRO, and tell if most of the
vibration was at rotation frequency and if
there was any ‘high frequency’ present. This
was adequate, as most of the problems
were caused by unbalance due to wear.
Two methods were used, in the fi eld, for
balancing. The timed-oscillation method
required only a stop watch and graph paper
[1]. The other used a manually tunable fi lter
that fi red a stroboscope to detect previously
chalked numbers around the rotor. The
usual vector calculations followed.
Lesson 1 Choose your bosses well...
Lesson 2 and when a plant is new and/
or the major asset makes it
easier to get proposals for
monitoring etc. accepted.
In 1966, after further training attachments, I
was assigned to Hazelwood Power Station.
Figure 1 Cross-section of 200MW generator that proved to have loose bore plugs
maintenance & asset management vol 26 no 2 | ME | Mar/Apr 2011 | 49
hole packed tightly with rubber bungs.
Flaws were found in one of the rotors and
a length was bored to a bigger diameter….
but bungs of the same size were inserted
(see Figure 1). You can guess the effect of
these masses moving around! They were
removed – ‘no longer our practice’ – and
after an expensive 38 weeks off-line, all ran
well.
Lesson 3 Correct and confi dent
diagnosis is often possible
without complex instruments.
Lesson 4 Persist with the ‘5 Whys’ until
every possibility for a cause
has been exhausted - right
back to the intimate detail of a
component’s manufacture.
Case study 2 The coal mills (64 of them!) were essentially
a large heavy single-stage fan, driven
through a fl uid coupling. The coal fl ow
eroded the blades unevenly, causing
unbalance. Unlike the older much smaller
mills at the older Yallourn power station,
timed-oscillation balancing was not
workable and the phase angle method was
used.
A rough mill would be detected on routine
vibration checks, and arranged to be taken
from service. Next day it was cold, and was
isolated to be safe for phase marks to be
chalked around the drive shaft. De-isolation
was followed by an ‘original run’. Shut down
and isolated, a trial weight was attached
and a calibrating run made. Shut down
and isolated, the balance correction could
be made at the blade chosen. De-isolated,
a fi nal check run was made. Provided
operators were available, this took a day.
I decided to make permanent shaft marks,
and from records of our experience came
the rule: ‘Cut off one pound per thou of
vibration two blades behind the indicated
high spot’. A table giving size of cut and
mass was provided. Balancing now took
an hour or so, as the initial reading was
made on-line when the high vibration was
expenditure on test equipment that the
technical heads in the power stations had
ever seen. He did so on the condition that
each station provided an engineer to work
with me in applying the equipment. This
proved to be very wise, and gained the
‘buy-in’ at each place that a superstar would
not have gained working alone!
Lesson 6 If you fi nd that worthwhile
learning for your organization
can only be obtained outside
it (whether in another country
or not), make the proposal,
but ensure that it is only you
that can be selected to go!
Lesson 7 To get buy-in, involve locals
deeply in any development.
DOCUMENTED TEST PROCEDURES AND PROGRAMME OPERATIONI was assigned to the newest plant –
Yallourn W with two 350MW steam units
(now just called Yallourn) – and set up the
CM programme. Part of this was my belief
that documented test procedures are
essential, not only for our CM people, but to
get operating staff on side. We wrote about
25 of these documents.
[In 1987, I returned as a member of the
management team. The station now had
four units – two 375MW units had been
added. What had happened to the CM
work? I found that more test procedures
had been added – there were now 58!
The CM team was led by a keen technical
offi cer. We produced a regular newsletter
summarising our test work and results
(recommendations for urgent action did
not await its publication!). Never more than
one page long, 70 copies were distributed
throughout the plant. Operators, in
particular, commented favourably, as did
the plant manager, and at privatisation in
1995 the new owners found that the CM
team had better maintenance records than
the offi cial CMMS! Later, they won the CSI
award for best CM programme.]
Lesson 8 For staff training and for
briefi ng of relevant staff,
document the procedures
(include digital pictures) and
make then available to all on
the company intranet.
Lesson 9 To ensure continuity of the
CM program, estimate costs/
benefi ts and maintain a
running score sheet. Even
if only done for a sample
period each year, worthwhile
payback will be shown.
Publicise your activities
modestly, admitting any
shortcomings.
Lesson 10 Initial development of CM
Lessons Learnt in 45 Years of Condition Monitoring
detected. The next day with the mill isolated,
open and cold the correction could be
made and the machine closed up for return
to service.
Case study 3 Routine testing of the boiler feed pumps
was done as at Yallourn, with throttling in on
the outlet valve to get head-fl ow test points
over the widest range allowable. This took
some time and much physical operator
effort. Refl ecting that internal wear has a
consistent effect to the head-fl ow curve, I
realised that throttling was unnecessary,
as one or two points around the normal
operating area were enough. Testing now
takes 15 minutes per pump [2], and later
plants take advantage of their distributed
control system (DCS), see Figure 3.
Figure 2 Large lignite coal mill (eight per boiler)
Figure 3 Boiler feed pump (4500kW): head-fl ow data logged by DCS (truncated diagram)
Lesson 5 Review test procedures
regularly, to fi nd if a test or
procedure is, in fact, still
needed, or can be simplifi ed
or have its interval stretched.
THE UK EXPERIENCEBased on my proposal to learn more about
condition monitoring I was successful in
getting a two-year travelling scholarship
to work in the UK. (500MW boiler
commissioning with Babcock, turbine
design and dynamics with Parsons, and
tests and investigations with the then
CEGB). Unlike my home situation, with the
world’s cheapest fuel, thermal effi ciency
was the priority, but its engineering effort
shares much with condition monitoring.
Following a shaft crack in a 500MW unit,
vibration monitoring had been further
developed.
I returned full of ideas, and wrote
eleven reports. Only one had a specifi c
recommendation to spend money,
viz. to enhance our vibration analysis
capability by obtaining a real-time analyser,
accelerometers, vector fi lter phase meter,
plotter, tape recorders, etc. The power
generation manager approved the largest
50 | Mar/Apr 2011 | ME | maintenance & asset management vol 26 no 2
applications is well done or
managed by professional
engineers, but ongoing
routine CM is better run by
technical staff whose career
expectations are likely to be
less ambitious. Trades/craft
people can also fi nd this a
fulfi lling career.
IN THE MEANTIMEIt took some months to write specs, call
for bids and then analyse them and place
orders. In my absence the Yallourn (old
station) people had bought a replacement
balancing instrument. It had a signifi cant
advance on the old ones – it had a
frequency scale! Without them realising this
capability, we had a way of fi nding vibration
signatures (spectra). Several intractable
vibration problems were solved [1]. I recall
the stores manager raising his eyebrows
when asked to locate a large mill bearing
and count the number of rollers in it!
Lesson 11 Check your cupboards – you
may have under-utilised
equipment with as yet
unknown capability! See
again Lesson 3.
PUTTING THE ADVANCED VIBRATION ANALYSIS EQUIPMENT TO WORKNo single supplier could provide all the
items we needed (this was in 1975). By
connecting vibration transducer to signal
conditioning to analyser to plotter it was
easy to get a one-off vibration signature. But
as our aim was to start routine signature
analysis, repeatability was essential. After
some experimenting with signal outputs,
gain and attenuation, this was achieved.
The operating instructions were apparently
written by the electronics design engineers
and were diffi cult to understand by us
mechanical types! I wrote a handbook
of simple step-by-step instructions for
applying all the equipment. An example is
shown, in Figure 4, of the RTA front panel,
showing the required buttons and dial
settings.
We designed a special graph paper so that
plots could be compared by holding sheets
up to the light. Our intent was to eventually
have this comparison done by a computer,
but in the pre-PC days….
As the equipment was to be shared around
fi ve power stations, we set up clearly
labelled carry cases to facilitate collection
by any driver. Each case had the required
connecting cables. Unfortunately, after
some time cables got lost. Locating the
cases also took time. In the ensuring years,
more advanced FFT analysers, multi-
channel tape recorders, and later versions
of other instruments were obtained. A major
re-organisation set up a central specialist
group.
Lesson 12 Specialist test
equipment needs
to have a regular
owner and full-
time skilled operator
Hand-portable analyser/collectors and
associated computer packages have now
become commonplace, so our dream has
been realised.
Case study 4 Via the long cable reel, the new graduate
engineer hooked up the accelerometer to
the signal conditioning/readout instrument.
He reported that turbine vibration was
55mm/s rms – over ten times greater than
what might be expected! Before panic
set in, we found that he had used the
cable to connect the accelerometer to the
instrument. It was an ordinary shielded
co-axial type, intended to be used from
the instrument to an analyser. Low noise
cables are required from charge output
accelerometers to avoid tribo-electric
boosting of the output to give a spurious
high vibration reading.
Lesson 13 Check, and re-check, critical
data values if any look to be
unusual.
Case study 5 Using an innovative approach, site trim
balancing was conducted on a 120MW
generator rotor. The coupling between
turbine and generator was unbolted,
and faces held apart. The exciter was
connected to run as a motor, with the
rolling torque provided using the overhead
crane and a rope wrapped around the
rotor. (Appropriate design checks had been
made).
After reassembly, run-up proceeded as
normal until, when nearing normal service
speed, generator bearing vibration suddenly
jumped so much that the fl oor shook and
dust fell from the rafters! The operator
tripped the machine. Subsequent attempts
at run-up were no different. A challenge for
the vibration team! The gear was set up with
the analyser set to PEAK HOLD mode. The
extreme vibration was revealed as at 19 Hz –
the fi rst critical speed of the rotor.
Figure 4 Front panel of the analyser showing how to set it up (from the operating handbook we wrote).
It was noticed that the vibration started
soon after the auxiliary oil pump was
stopped, so it was left running and the
unit was eventually put into service. The
19Hz vibration was still evident, and could
be varied in amplitude by changing the oil
temperature.
Bearing dimensions and clearances
were found, and the bearing wedge
pressures (giving shaft loading) and oil
temperatures noted in order to calculate
the Load Parameter. As shown in Figure
5, the resulting plot on a bearing stability
assessment chart showed that the
operating range was well outside the
‘recommended’ area [3].
The only variable that could be changed
permanently was the ength of the
bearings (to increase the specifi c loading).
Surprisingly, the spares in the store were
found to be shorter, as were those on
maintenance & asset management vol 26 no 2 | ME | Mar/Apr 2011 | 51
the adjacent ‘identical’ machine! Bearing
changeover was the cure. This was a
strange case, as this machine had operated
for seventeen years without this problem.
The vibration team gained superhero status
for this success [4].
CM BY PERFORMANCE ANALYSIS – THE BIG BUCKS
Case study 6 I had developed performance tests, with
useful outcomes, for both types of 200MW
machine at Hazelwood, and continued this
at Yallourn W, the methods followed having
subsequently been published [5]. On one
unit our tests were run before the offi cial
acceptance tests.
Routine tests on a 350MW unit showed a
small but signifi cant decline in performance.
Prior to a planned outage, a steam forced
cool was conducted. This procedure is
used to bring the machine to standstill more
quickly by cooling the turbine metal, rather
than allowing slow natural cooling. The inlet
steam temperatures were slowly decreased
over some hours during offl oading. Testing
after return to service showed that the
performance had returned to its initial level.
Close examination of the data led to the
conclusion that there was some restriction
in the intermediate pressure section,
deduced to be from blade deposits [6].
Soon afterwards, the OEM site manager
met with the plant manager to tell him that
as the fi rst unit had reached two years
of service, it was time to arrange a major
outage and strip-down. When asked the
reason for the recommendation he was
told that an inspection after two years was
standard practice in the OEM’s country. The
manager had been my boss and mentor
in my initial job, so was well versed in CM!
He did not support an overhaul given
our vibration and performance condition
assessment, and the machine continued to
operate for seventeen years before its high
pressure section was opened.
Lesson 14 Take OEM recommendations
into careful consideration, but
do not follow them blindly.
Case study 7 In 1995 tests run on a 500MW turbine
at the latest plant (Loy Yang B) led to an
overhaul to remove metal debris carried
from the boiler. Long experience elsewhere
had shown that accurate special tests
were needed to obtain CM data, as plant
instruments were neither suffi ciently
accurate nor repeatable.
As this plant had a DCS opportunity had
been taken at each accurate (and high
cost) ‘Valves Wide Open (VWO)’ test to
extract data from the plant historian and
compute the same condition parameters.
Although the same values were not
obtained, a directly comparable trend was
clear, as shown in Figure 6 which shows
the VWO trend over its life from its initial
acceptance test.
Lesson 15 Assess whether the plant
instruments can be used to
give a usable trend for CM. If
a DCS exists, then try data
extraction and utilisation.
Case study 8 The superheater tubes in a series of large
coal boilers of the same natural circulation
drum type design leave the furnace through
spaces between roof tubes, and connect to
later sections, often via headers. There are
several superheater sections in series. The
platen superheater at the top of the furnace
has thirty sections, each with sixteen tubes
in a U-shaped pendant loop, hanging
through the roof tubes of the furnace. Unlike
other designs, where the leading tube down
has a kink so that it becomes an inner tube
in the up direction, these pendants are laid
out such that the assembly would be fl at,
i.e. the inner tubes are progressively shorter
than the outer tube. The platen is heated
mainly by radiation, so the longest tubes
on the outside of the array take up more
heat than those on the inner side. These
tubes are then led out of the furnace space
through gaps in the roof tubes into the
dead space, where they connect to primary
superheater inlet tubes. There are eighty of
these superheater sections across the gas
path, so each has six tubes.
Excessive metal temperatures lead to
considerable reduction in creep rupture
life. At these temperatures an increase of
Figure 6 Comparison of accurate tests (upper plots) with results calculated using DCS data (lower more numerous points)
Lessons Learnt in 45 Years of Condition Monitoring
Insert Figure 5 Bearing stability chart showing eff ect of oil viscosity and bearing length
52 | Mar/Apr 2011 | ME | maintenance & asset management vol 26 no 2
the furnace wall rather than specifi c tube
numbers. The lesson here is to check such
points in detail if two ‘identical’ plant items
show quite different behaviours [8].
Lesson 16 In critical cases, do not
believe everything you read
in the control room without
verifi cation of labels and
actuality at and inside the
plant.
CONCLUSIONS AND FINAL LESSONSCondition monitoring can be a key
contributor to higher reliability and availability
when set up properly and run by trained
and dedicated people. Some investment is
needed in equipment but much useful work
can be achieved with simple instruments.
Lesson 17 Training is essential before
starting CM work, followed
by regular reinforcement
via courses, conferences.
Consider getting certifi cation
to verify capability.
Lesson 18 Share your learning via on-line
forums, conferences, articles
in engineering magazines.
Lesson 19 Make recommendations clear
and concise: put the technical
complexity in appendices.
only 11°C can halve the life, so operational
monitoring is important. Manufacturers
use thermocouples installed in tube walls,
sometimes in special sections, to try and
measure the maximum metal temperature
[7]. Such sophistication was not available
when these boilers were built so, at several
sections, fi ve thermocouples were fi xed
across the gas path to primary superheater
outlet tubes in the dead space, and the
limits for operation derived by calculation.
Two boilers built almost at the same time
exhibited quite different temperature
behaviour at otherwise similar operating
conditions. One was often close to alarm
limits, and operation was adjusted to keep
within them. The other showed no such
high temperatures. After some years of
service the ‘good’ boiler suffered a spate of
superheater tube failures due to overheating
and creep rupture, and the complete
superheater had to be replaced. Why
should two identical boilers be so different?
Close investigation and painstaking
tracing of tube path layouts showed that
the hottest tubes from the outside of the
platen array led mostly to leading tubes,
but sometimes to the tube behind it in the
primary superheater, as the number of
platen tube banks is less than the number
in the primary superheater. The monitoring
thermocouples were installed on leading
tubes. Unfortunately, in the ‘good’ boiler, the
thermocouples were installed on leading
tubes that did not come from the hottest
tubes out of the platen. Presumably, the
installer was given set distances in from
Lesson 20 THE MAJOR ONE. Condition
monitoring is not an end in
itself, and should be applied
along with other maintenance
strategies as decided by an
RCM or similar analysis.
REFERENCES
1. Beebe R, Machine condition monitoring, MCM Consultants, Hazelwood, 2001
2. Beebe R, Predictive maintenance of pumps using condition monitoring, Elsevier, London, 2003
3. ESDU 66023, Calculation methods for steadily loaded pressure fed hydrodynamic journal bearings, Engineering Sciences Data Unit, IMechE London, 1966
4. Beebe R, Diagnosis and solution of resonant whirl on a steam turbine generator, Proceedings ICOMS2002, Brisbane, 2002
5. ASME, Simplifi ed procedures for routine performance tests of steam turbines, ASME PTC 6S Report, 1970. (Re-affi rmed and revised 2003)
6. Beebe R, Recent experience with condition monitoring of steam turbines by performance analysis, IEAust Mechanical Engineering Transactions, pp 42 – 49, 1978
7. BEI (British Electricity International), Modern power station practice: incorporating modern power system practice (3rd Ed), Oxford Pergamon Press, 1990-1992
8. Beebe R, Is your control room data telling you what you think it is? Maintenance and Asset Management, Vol 22, No 3, 2007 (and other journals)
ABOUT THE AUTHORRay Beebe has a passion for condition
monitoring acquired from 28 years in
power generation, followed by 18 years
at Monash University where he led the
postgraduate (off-campus learning)
programmes in maintenance and reliability
engineering. Since retiring from tenured
service he continues teaching and
speaking involvements and is working on
a third book. He was awarded Engineers
Australia’s 2004 George Julius Medal for
his second book Predictive Maintenance
of Pumps using Condition Monitoring. He
has spoken at conferences world-wide,
and his many papers have appeared in
technical journals. He can be contacted at:
His papers are available on request. A
complete list can be found on –
http://www.gippsland.monash.edu.au/
science/aboutus/people/academics
raybeebe.shtml
Figure 7 Boiler cross-section above furnace.