Boiler Tube leakage
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BTL
NoUnit Trip date
Synchro
Date
BTL
AreaOutage hrs MU Lost
SD Oil
(kL)
Start Up
Oil (kL)
Outage
Cost
(crores)
1 226-04-2010
11:53
01-05-2010
05:15Mid RH 113.37 34.01 6.65 130 6.36
2 105-05-2010
03:01
06-05-2010
17:58
Bottom
ring header38.95 11.69 5 90 2.42
3 116-06-2010
02:42
22-06-2010
12:48LTSH 154.10 46.23 54.45 165 8.82
4 203-07-2010
07:13
06-07-2010
01:33
Econo -
miser66.33 19.9 11.5 149 4.12
5 1 16-07-201018:10 21-07-201004:23 LTSH 106.22 31.87 10 118.8 5.976 2
20-01-2011
22:48
23-01-2011
08:12LTSH 57.40 17.22 4 110.5 3.45
FIN YR TOTAL 536.37 160.91 91.60 763.30 31.14
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BTL
No
UnitTrip
date
Synchro
Date
BTL
Area
Outage
hrs
MU
Lost
SD
Oil
(kL)
Start
Up Oil
(kL)
Outage
Cost
(crores)
1 208-05-2011
23:26
13-05-2011
05:25LTSH 101.98 30.595 1.65 122 5.73
21
13-06-2011
13:17
16-06-2011
01:09
Water
Wall59.87 17.96 3.3 54.45 3.29
3 226-06-2011
20:41
01-07-2011
08:14
Water
Wall107.55 32.265 1.65 117.15 5.98
41
01-08-2011
17:09
05-08-2011
05:41 LTSH84.53 25.36 1.65 99
4.74
5 221-11-2011
23:19
25-11-2011
14:21LTSH 87.03 26.11 16.5 126 5.07
FIN YR TOTAL 440.97 132.2924.75 518.60 24.82
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BTL
NoUnit
Trip
date
Synchro
Date
BTL
Area
Outage
hrs
MU
Lost
SD Oil
(kL)
Start Up
Oil (kL)
OutageCost
(crores)
1 218-04-2012
23:51
22-04-2012
13:30Near IK 36 85.65 25.695 37.95 110.55 5.10
2 125-04-2012
10:29
27-04-2012
16:06 Water Wall 53.62 16.085 6.6 97 3.25
3 228-04-2012
21:30
03-05-2012
02:44LTSH 101.23 30.37 6.6 112.6 5.72
4 103-05-2012
12:43
06-05-2012
13:52LTSH 73.15 21.945 6.6 80.85 4.14
FIN YR TOTAL 313.65 94.09 57.75 401.00 18.21
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FIN YR NO OF BTL
TOTAL
OUTAGE
HRS
TOTAL OUTAGE
COST
2010 11 6 536.3731.14
CRORES
2011 12 5 440.97 24.82CRORES
2012 13
(Till Date) 4 313.65
18.21
CRORES
TOTAL 15 1290.9974.17
CRORES
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BTL
No
Unit Trip date Synchro Date BTL AreaOutage Cost
(crores)
Preceding Trip
date
SD Cause Outage hrsDay
Difference
1 226-04-2010
11:53
01-05-2010
05:15Mid RH 6.36
25-03-2010
23:03
Mid RH Tube
leakage136.92 32
2 105-05-2010
03:01
06-05-2010
17:58
Bottom
ring
header
2.4203-03-2010
19:13
Furnace Clinker
Formation216.58 62
3 116-06-2010
02:42
22-06-2010
12:48LTSH 8.82
03-06-2010
10:47
Replacement of
40116 Isolator
contactor
4.95 13
42
03-07-2010
07:13
06-07-2010
01:33
Economise
r4.12
13-05-2010
23:00
Furnace
pressure LL6.58
50
5 116-07-2010
18:10
21-07-2010
04:23LTSH 5.97
10-07-2010
13:28Coal Shortage 30.32 6
6 220-01-2011
22:48
23-01-2011
08:12LTSH 3.45
15-12-2010
13:38
DCS Power
Supply failure63.93 36
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BTL
NoUnit Trip date
Synchro
Date
BTL
Area
Outage
Cost
(crores)
Preceding Trip
dateSD Cause
Outage
hrs
Day
Difference
1 208-05-2011
23:26
13-05-2011
05:25LTSH 5.73
01-05-2011
00:54
Condenser
Tube Cleaning80.82 8
2 113-06-2011
13:17
16-06-2011
01:09
Water
Wall 3.29
22-05-2011
04:04
Low system
Demand24.079 22
23-05-2011
14:14
Drum level
sensor malfunction
6.417
2125-05-2011
21:59
1SB - 1PAB 6.6kV
Breaker Earth Fault
tripping
5.783 19
3
226-06-2011
20:41
01-07-2011
08:14
Water
Wall5.98
18-06-2011
19:04
DCS Communication
failure4.95 8
21-06-201110:45
415 V Busfailure
3 5
4 101-08-2011
17:09
05-08-2011
05:41LTSH 4.74
16-07-2011
20:05
Furnace pressure
LL6.583 16
5 221-11-2011
23:19
25-11-2011
14:21LTSH 5.07
27-10-2011
09:37Coal Shortage 144.4 26
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BTL
NoUnit
Trip
date
Synchro
Date
BTL
Area
Outage
Cost
(crores)
Preceding
Trip date
SD
Cause
Outage
hrs
Day
Difference
1 218-04-2012
23:51
22-04-2012
13:30
Near
IK 365.10
16-04-2012
09:58
FICF
pressure
low
3.23 3
2 125-04-2012
10:29
27-04-2012
16:06
Water
Wall3.25
10-03-2012
09:33
Exciter
Brush
failure
60.73 46
3 228-04-2012
21:30
03-05-2012
02:44LTSH 5.72
25-04-2012
15:54
Aux
power
failure
3.25 3
4 103-05-2012
12:43
06-05-2012
13:52LTSH 4.14
25-04-2012
10:29
BTL
Water
Wall
53.62 8
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MAKING BTL ZERO!!
REPLACEMENT OF WEAKENED TUBES / JOINTS AT
THE EARLIEST OPPORTUNITY, i.e. WHEN UNIT TRIPS
DUE TO SOME OTHER REASON
REGULAR MONITORING OF METAL TEMPERATURE
EXCURSION
REGULAR MONITORING OF METAL TEMPERATURE
AT LEAKAGE PRONE AREAS e.g. NEAR
SOOTBLOWERS
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THIS CALLS FOR AN ONLINE BOILER METAL
TEMPERATURE MONITORING SYSTEM THATWOULD ENABLE
24 X 7 BOILER TUBE METAL TEMPERATURE PROFILING
IDENTIFICATION OF TUBES ON THE VERGE OF
LEAKAGE.
ASLDs HELP ONLY AFTER THE TUBE LEAKAGE HAS
OCCURRED
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To lower fuel cost, we change coal sourcefrequently resulting in frequent changes in
fuel quality. Differences in fuel cause
combustion changes that affect slaggingand soot deposition in the furnace.
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The conventional sootblowing techniques relies
on employment of a large number of smaller
sootblowing systems, activated by the personaldiscretion of the control engineer rather than
activation based on measurements.
The problems associated with a fixed scheduleblowing system:
1) Excessive blowing wastes steam2) Insufficient blowing decreases efficiency
3) Unbalanced blowing may cause opacity
spikes.
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Fouling and slagging in the furnace as well as in the
convective heat exchanger zone leads to a reduction
in boiler efficiency and reduction in availability such
as:
1) Increase of furnace backend temperature
2) Increase of attemperation rate
3) Damages in the hopper area and the wet/dry
bottom ash system as a result of big slag formations
falling down from the furnace walls or/and
superheater.4) Unplanned boiler shut downs
5) Overcleaning damages tubes, affecting unit
availability
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FOULING IN FURNACE AREA
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ACCUMULATION OF COARSE ASH &
SLAG AT Bottom ash Hopper
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Therefore the solution is to blow appropriate
sections of the furnace as needed.
THIS CALLS FOR INTELLIGENT OR
SMART SOOTBLOWING SYSTEM
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SMART SOOTBLOWING LOGIC
source: EPRI
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BENEFITS OF SMART SOOTBLOWING
Reduction of tube erosion Reduction of usage of water
Reduction of attemperation spray rates
(extension of tube lifetime) Reduction of backend temperatures.