AQ_F_0100237_20190910_ST_STO-Rpt (4)

NORTH CAROLINA DIVISION OF Winston-Salem Regional Office
AIR QUALITY Canfor Southern Pine-Graham Plant
NC Facility ID 0100237
Stack Test Observation Report County/FIPS: Alamance/001
Date: 09/13/2019
Facility Data Compliance Data
Canfor Southern Pine-Graham Plant Observation Date: 09/10/2019
4408 Mt Hermon-Rock Creek Road Observer's Name: Thomas Gray
Graham,NC 27253 Operating Status Operating
Lat: 35d 58.8660m Long: 79d 25.0320m Action Code 23/STACK TEST
SIC: 2421 /Sawmills&Planing Mills General OBSERVED
NAICS: 321113/Sawmills
Contact Data Permit Data
Facility Contact Authorized Contact Technical Contact Permit 06740/T22
Kristie Hill Mark Blalock Kristie Hill Issued 9/6/2019
HR Manager Plant Manager HR Manager Expires 4/30/2023
g g(336)376-5803 [phone] [phone] Classification: Title V
Permit Status: Active
Inspector's Signature: 1/�/y�\ '�` Comments:
Date of Signature: MTH
Emission Sources:
Emission Emission Source Description Control Control Device Description
Source ID No. Device ID No.
B-2 One wood fuel-fired boiler(28.7 MC-2 Two multicyclones(16 nine-inch diameter tubes
NSPS Dc; million Btu per hour maximum heat MC-2A and 44 six-inch diameter tubes,respectively)
Case-By-Case MACT' input capacity)
MACT DDDDD2 ESP-2* One electrostatic precipitator
B-3 One wood fuel-fired boiler(28.7 MC-3 Two multicyclones(16 nine-inch diameter tubes
NSPS Dc; million Btu per hour maximum heat MC-3A and 44 six-inch diameter tubes,respectively)
Case-By-Case MACT 1 input capacity)
MACT DDDDD2 ESP-3* One electrostatic precipitator
B-4 One wood fuel-fired boiler(57.6 MC-4 Two multicyclones(36 nine-inch diameter tubes
NSPS Dc; million Btu per hour maximum heat MC-4A and 44 six-inch diameter tubes,respectively)
Case-By-Case MACTi input capacity) ESP-4* One electrostatic precipitator
MACT DDDDD2
Introduction:
On September 10,2019, Mr. Davis Murphy,Environmental Engineer/Permits Coordinator of the Winston Salem Regional Office-
Division of Air Quality(WSRO-DAQ), contacted Ms.Kristie Hill, HR Manager, of Canfor Southern Pine-Graham plant, for the
purpose of observing stack testing being performed on the facility's wood fired boilers(B2,B3, B4).All three boilers are controlled
by two multicyclones and an electrostatic precipitator, each.The boilers have heat input capacities of 28.7,28.7 and 57.6
MMBtu/hour,respectively.Testing was performed to demonstrate compliance with 40 CFR Part 63 Subpart DDDDD, "NESHAP for
Major Sources: Industrial, Commercial, and Institutional Boilers and Process Heaters."listed in permit condition 2.2.C.1. Also,
Boilers B-2,B-3, and B-4 are subject to 40 CFR 60 Subpart Dc,"Standards of Performance for Small Industrial-Commercial-
Institutional Steam Generating Units,"listed in permit condition 2.1.A.4 and 15A NCAC 2D .0504,"Particulates from Wood Burning
Indirect Heat Exchangers,"listed in permit condition 2.I.A.I (B-2 and B-3 only). Tyler Mills,of TRC Environmental Solutions,was
the leader of the test crew performing the sampling.Other members of the test crew included Brad Ourts and Alex Johnson. Testing
1

was conducted over the course of three days. Mr.Murphy observed testing on the first two days(9/10-9/11)while Thomas Gray,
Environmental Specialist,also of the WSRO-DAQ observed the third day(9/12).
Test Methods:
On April 15,2019,the WSRO received a protocol submittal form(PSF)indicating the facility wanted to conduct testing May 14,
2019. Testing was subsequently delayed. The proposed test methods are listed below.
EPA Test No.of Test Run No. Sampling
Target Pollutant. Method Test Runs Duration. Points Comments
Stack gas flow rate,moisture 1,29 4 3 Sampling points determined
O2/CO2 3A by Method 1 verification
CO 10 90 Minutes See Comment including absence of cyclonic
Filterable PM 5 3 (See Note) flow determination and
HCl 26A Method 7E section 8.1.2
Mercury,- 30B stratification test
The PSF was forwarded to SSCB on April 16,2019 and subsequently approved by the SSCB on May 8,2019. It is noted that the
protocol approval letter states that the facility will perform HCl-equivalent testing,however the Subpart 5D does not require this, so
the facility will only be testing for HCl.
Testinp,:
Testing began on September 10,2019 on Boiler 3. Method 1 criteria was met on each boiler,with maximum sampling points being
performed on each boiler(24 points). To ensure minimum detection limits were met for the 30B sampling,test runs performed were
90 minutes in duration. Being that each stack had two ports,and 24 points were being traversed, each point was sampled for 3.75
minutes each(90 minutes/24 points=3.75 minutes per point).Methods 2 and 4 were performed in conjunction with the Method
5/26A train,and Method 3A for O2/CO2 and Method 10 for CO were completed using a CEMS system.
Applicable Limits:
Emissions Standard Pollutants Limits Notes
40 CFR 63 Subpart DDDDD National Emissions Filterable PM 0.037 lb/mmBtu
Standards for Hazardous Air Pollutants for Major HCleq 0.022 lb/mmBtu May 20,2019 Applicability
Sources:Industrial, Commercial and Institutional CO 3-hr ave) 1500 m 3%02 Date
Boilers and Process Heaters Hg 5.7E-6 lb/mmBtu
Filterable PM 0.27 lb/mmBtu
HCleq 0.02 lb/mmBtu Applies through
15A NCAC 2D .1109 Case-by-Case 1VIACT 112j CO B-2, B-3 269 m 7%02 May 19,2019*
CO(B-4) 508 m 7%02
Hg 5.0E-6 lb/mmBtu
40 CFR 60 Subpart Dc Standards of Performance for
Small Industrial-Commercial-Institutional Steam Filterable PM 0.03 lb/mmBtu B-4 only
Generating Units
15A NCAC 2D .0504 Particulates From Wood Burning Filterable PM 0.45 lb/mmBtu B-2 and B-3
Indirect Heat Exchangers
*-No longer applicable
Method 5/26A-
The Method 5 and Method 26A sampling were performed in conjunction with each other.TRC used a Teflon filter support,glass
probe liner/nozzle,and probe and filter bell temperatures were maintained between 248-273 degrees Fahrenheit to meet the
requirements of both Method 5 and Method 26A.The Method 5/26a testing was performed by sampling the stack gas isokinetically
with the filterable pm being captured in the front half M5 filter,the hydrogen halides being captured in the acid impingers(charged
each with 100 mL 0.1 N H2SO4),and the halogens captured in the basic impingers(each charged with 100 mL0.1 N NaOH). It should
be noted the testers used a split train, in which a jumper was used from the filter box to the first impinger. Following the sampling, and
the post run leak check,the probe,nozzle, and front half filter bell were rinsed and brushed in triplicate with acetone and captured in a
250 mL amber sample bottle.The jumper used during the testing,was rinsed with DI water to ensure all sample was recovered in
impingers. The front half prepared M5 filter was then recovered and sealed in a labeled petri dish.Both the acetone rinse and filter
will be analyzed by gravimetric analysis. The impingers were then weighed gravimetrically for moisture analysis(M4). Then the
2

back-half filter bell, as well as the acid impingers and connecting glassware,were rinsed with 100 mL 0.1 N H2SO4 and combined in
a 1000 mL PE bottle for analysis by IC(Ion Chromatography). The same recovery was performed for the basic impingers,however
using NaOH. Mr. Gray discussed with Mr.Mills that HCl analysis was only required,Mr.Mills stated they would be archiving the
NaOH samples.At the time of the testing,no audit samples for HCl were required. Per the EPA emission measurement center
technical support page,"the general provisions to 40 CFR Parts 60 and 63 (see §60.8(g)(1)and§63.7(c)(2)(iii)(A))require that the
owner or operator obtain audit samples if the audit samples are"commercially available"and have defined"commercially available"
as two or more independent accredited audit sample providers(RASP)to have blind audit samples available for purchase." Since there
are no longer two providers,the requirement to obtain these audit samples is no longer in effect until such time as another independent
AASP has audit samples available for purchase.".During testing of B-4 on September 10,the post-run leak check failed on the second
run. The testers found the leak in the filter box, and believed it was due to a fitting that came loose when the probe was removed from
the stack.Nonetheless,the run was repeated,resulting in four test runs for boiler 4. On the same day,the nozzle was replaced on the
first run because the nozzle was damaged during a port change. A leak check was performed in conjunction with the equipment
change. On September 11 during testing of B-3,the method 4 condenser exit temperature momentarily rose above 68'F during the
start of run 1 and during run 2. Ice was added to the train and temperatures returned to<68.The temperatures did not exceed 72. Other
than the noted exceptions,methods were observed during the Method 5/26A testing,and all nozzle and pitot leak checks were within
method allowances. Isokinetics were maintained between 90-110%for all runs on all three boilers. The meter box utilized for this
portion of the testing had a gamma of 0.9969,and a delta H @ 1.86. See NC Source Observation Method 5 Checklist included below.
Method 30B-
Method 30B for elemental and oxidized mercury(Hg)was also performed on the three boilers. Method 30B was performed by
extracting a known volume of stack gas through paired in stack carbon sorbent traps,using a heated 30B sampling probe(heated
sufficiently to prevent condensation in traps). The method required paired train sampling to determine measurement precision and
verify validity of test results.The method requires a field recovery test which assesses the recovery of an elemental Hg spike with a
(90-110)%spike recovery required for run validation.Each sorbent trap consists of two separate carbon sections for breakthrough
analysis.The method requires under normal circumstances that breakthrough be less than 10%of the front half value,for the run to
be considered valid. Paired traps are also required to have a relative deviation(RD)of less than 10%for Hg concentration
<0.1 µg/dscm,and less than 20%RD for Hg concentration<.20 µg/dscm. 30B sampling was performed on all 3 boilers with an ESS
instruments 30B box that had an A side gamma of 1.0045 and a B side gamma of 0.9877 used on boilers 2 and 3, with an ESS
instruments 30B box with an A side gamma of 0.9850 and a B side gamma of 1.0003 used on boiler 4 .B side spiked tubes
(provided by Ohio Lumex)had a concentration of 50 ng,with the average sampling rate for both sides being 0.5 LPM,with a final
target volume of 45 L.As mentioned above,test runs were 90 minutes in duration to ensure the minimum detection limits of the
method were met.No deviations from the method were observed during testing of all three boilers.
Methods 3A and 10-
Method 3A for 02/CO2 and Method 10 for CO were performed in conjunction with the above-mentioned methods on all 3 boilers.
Stack gas was extracted through a heated CEMS probe through an out of stack filter,followed by a heated sample line(maintained
248 degrees Fahrenheit plus)to a sampling conditioning system,were it is dried before entering the analyzers. All direct
calibrations,bias,and drift checks were within method allowances(Direct Cal<2%of span,bias<5%of direct cal response, drift
<3%of initial bias and final bias). All calibration gases were verified as EPA protocol 1 gases,with expiration dates on all gases
verified to be within range.A CO span of 4376 PPM CO was used on all three boilers,with an 02/CO2 span of 22.15 and 19.47,
respectively, also used.No deviations from the methods were observed during the testing of all three boilers. Calibration data and
bias information are provided in the NC DAQ CEMS Observation checklist provided below.
Preliminary Results and Runtimes:
Boiler 4 M4):
Testing Performed on September 10,2019. Observer: Davis Murphy
Run# Run Time CO m dv CO 3_percent Oxygen m dv
1 11:30-13:19 300.437 444.82
2 14:11-15:53 348.561 537.40
3 void void void
4 297.264 442.61
Aver a 315.420 474.94
3

Boiler 3 W :
Testing performed on September 11,2019. Observer: Davis Murphy
Run# Run Time CO mdv CO 3 percent Oxygen mdv
1 12:00-13:36 732.095 1116.9
2 14:3 0-16:05 652.438 977.21
3 16:45-18:20 643.317 918.22
Averse 675.95 1004.11
Boiler
Testing was performed on September 12,2019. Observer: Thomas Gray
Run# Run Time CO(ppmdv) CO nu,3 percent Oxygen
(ppmdv) -
1 08:3 5-10:12 301.177 477.97
2 10:55-12:30 341.706 509.58
3 13:15-14:50 325.579 518.03
Avers e 322.82 501.86
Process Information:
Process information for each boiler was recorded every 15 minutes which included the following parameters: steam pressure, steam
flow, sawdust reading count,multicyclone OP, and opacity(measured by COMB). These parameters are used in the Method 19
calculations for heat input.Preliminary calculations indicated the facility was above the 90%maximum heat input for each boiler.
Being that the boilers are equipped with electrostatic precipitators,primary and secondary voltage readings were also recorded for
Fields 1 (B2-B4)and Field 2(B4 only).
Conclusion
Preliminary results indicate compliance with the CO limit.However, compliance with the HCl and particulate limit will be
determined upon analysis of the samples at the laboratory. The test report will be due to the WSRO-DAQ by October 10,2019. The
tracking number for this test is 2019-129ST.Attached below are the NC DAQ CEMS and Method 5 Observation Checklists.
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NC DAQ Source Test Observers Checklist-Particulate Testing EPAs.Methods 1-5
Facility Name/Location:
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Source Contact/Phone#: .
60,
Testing Firm/Contact:
: : AidFacilit ID Source/Tetel
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Tracking Number: 'o/— I Z-q ST
Test Date: 0/ l l Image courtesy of the EPA`"
sk for an explanation to any question answered"No"and attach comments to this form or in your report.
t
1.1)Method 1 calculated correctly(see reverse.side)? `
1.2)Cyclonic flow check completed during test day?(Average of absolute value of all angles<20 degrees?) t
,11 :! Kom=
2.1)Pitot tube leak check completed after each run? (� / •�
2.2)Visual check offpitot tube heads-good condition?
2.3)Manometer level and zeroed correctly?
2A)Static pressure measured during.the test day? Static Pressure: inches H2O
2.5)Barometric pressure recorded and adjusted for elevation?(see reverse side)
2.6)Pitot tube heads.oriented'to axis of flue?/Pitot tube perpendicular to axis of stack?
2.7)Temperature recorded at each sampling point?
2.8)Minimum sample of 30 dscf collected(or,per applicable subpart?)(see Vm above)
,w r
3.1)Is molecular weight being assumed?(If yes,and allowed,skip rest of Method 3)(see reverse side)
3.2)Multi point integrated sample/Bag evacuated and leak free(if applicable)
3.3)Electronic Analyzer;or Orsat(performed in triplicate,analysis consistent?)(circle)(see reverse side)
3.4)Calculate F0/Within Range?
F
4.1)100 ml H2O in first 2 impingers,3rd.empty,silica gel in 4th?(see reverse for each impinger design req.)
4.2)Temperature at the exit of impingers/condenser<68 F?(see reverse side)
4.3)Silica gel in good condition?-Blue-new,Pink-spent(unable to absorb more H2O)
F
5.1)Methods 2-5 run concurrently?Test team accurately recording meterbox data at each sampling point? C
5.2)Visually inspect sample nozzle for damage/nozzle opening facing direction of flow?
5.3)Pre run leak check,optional(watch)Leak Rate 50.02cfm? I- vl' 11110,
5.4)Post run leak check,mandatory(watch)Leak Rate 50.02cfm?Conducted>_highest vacuum during run?
5.5)Isokinetic rates be 90%and 110%o?(see reverse side) K factor: ,. / �� !y
S.6)Filter and probe temperatures at 248 25F(or applicable subpart,such as-MA S)? "
5.7a)During a run,was any equipment changed(ie.filter,nozzle,impinger)Why?(Do not explain a"No") UZzl
5.7b)Was a leak check performed prior to the equipment change?(May not be applicable)
5.8)Meterbox calibration values AH@: 1,, Y:0..'::1`'4;G Date Calibrated:
5.9a)Particulate sample clean-up:acetone used?(or water if required by CFR such as MALT MM)?
5.9b)Inside of nozzle,probe,and glassware(before the filter)rinsed and brushed in triplicate(minimum)?
5.9c)Is filter holder disassembled on site or transported to lab intact?(circle)
5.9d)200 ml acetone blank prepared? Volume of acetone used for cleanup:
5

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(final�wsmm cal.-Initial y xtetr,cal),span I WO. All caliltralion,gam si 11 be used for the(%libratirm er,t�x t..t, t?stlu the zero aatc3 aanc-sit ps am rcqpirW Rs tt stem ca�ikrm-ioos
v
„ {
N

oi 2 28.7 M:MB-tu/lir Rat.-ed Heat Input
D e
20 F
,,700 Rated St:ea.1.1i'low
Test Date:
M ulticii ne
0 ressu Xyg..e.n IM... :p
-dust Readin Op e Drop.. ESP Zon e 1
Steam Pressure Steam Flow Saw 9 TRIM : .
AC Initial-S;Count
Time ps"I ---------- ................... 10.)............................. ............
............................................. ............................... .................... ..................................................................................................... ----------- ... -----------
----------- .......... ..........
C
75 7� . 2 55 TB1232. .1 I51 5�fi .6
.......................
193
157-4121,76 5 5:T B.......
5-.9
..........................
3:50 1: 5:5:TB
.1,574'.460 53 i6l
.8800:213.4: .......... .................. ........
................... ................. .............................. ........
5.2
55:TB
17000 -15,41633 1.44 2.8
TB
12: 355
9,3 15 .19,80G, .1.5741851 1.47
......................................... ............................................... .....I...........
................................ ...........................................................................................
.......................
-5.5 TB
51 144;
:5 7 4.210 6
S:5 4,3- 12'33 4.0400: 355,
55:
.4
C 0 '15742-2-39 L5.: 2 14
1841D 4 ........................................ ............
VO...
S.:
3.1.T 5.8. 355
18743: -......
90.5%steam load
R.-Un 2 .........
5.5-TB
41
15742897
5 -- M............ ......................... ........
122.1. 21330
..........- ........ ...................................................................................................
.................. ........................... ........................ ...... A C
354: 55:TB
5743
....................
..................... .............................
............. ............... .........................
359
25741501 :TB
13. 4 4.8
.......................... ...................................
20400* ...............
12-3.--0
................................ ...............................................
................................................
4.:8 357 55 TB
1.-,;44 6.1
157.4-351.6
11:40 122-7 21600:
............ .........
5.5.TB
........................
20 1574364-.-- 51 4 3.5.6.................
...... dw.
.............................................. ...............................
....... .................................... .......................... 55:
5�6 TB
4.:8
1173 119,700:
15743893 IAG
4.6
.................
117.0 19400: 157-44-1-01 1,43: 6.4
----------------
1,42: 6.1 4.7 3.57 -55
AVERAGE1.20.16 20276. .......... ...... ........................................................ ......
.................................................
98.01%steam toad
R u t',3 .................................. ............. ......................................
... ......................
.....................
....... 55,
359:
13.:-1.5, 11 .0 1`931 10: 1574474.6 135.
A
5.5.TB
12-3.7 60Q 57.44,966
!D,,zi 125-2. 1-S.,7 10:: 157,45113-8 1 5.,6 35.9.:............. TB
..........
..................... .........
..........
.....................................
........... 4.8
351 55:TB
1 1,4-5: 5,5.
I'A-:00 15745317 ......
..............
.................... ...
55:TB
EK,
12.3-1. 17900:: 157-455,07 133: 4.6 . ................................
--------- .. .............................. ---------------------------------------------
55,TB
A
1-43 125.7 .18880: 157-45710 111: 6.14 4�6 58
............ ...............
. . ............................ ...... . ................
2 41 5--T�B-...
6.3
14:.4 5 1 18400: 1:5745,30 1...29::
-4.8: 355 55
AVERAGE 19014: 1.35 ....... ..................... ........
...........
team load
steam load
13

Canfor Southern Pi-ne-Grah-am Plant
Stack.Test Log She-et
6 ofler 3 29.7 M...Wt.u./fir Rated Heatitiput
207 :
.0,0.'R:ated Stea.--rn Flow
T e st Datl,z
Multi-Cf.-one
EISP Zon.-e 1-es. ',tea t"..1 �P rap.
Savvdus-t 0 acity Oxyg-..en Tr-."* reSsuf--Ve D.Steam:Pr -s-ure III Flow
T r................e............................ P5............................. I :/-h -------- .................. COnt, .......... ---------- ...... % ...... --------%-------------..........- H0--
----------------- C--------- ..........
RunNumber
............................- .....
12:1005...................................................11....22...2.3....-..07 ........................................1'1...77.... 96 ...............................-5 S 5 1 091 MR 185:: ................... ............................56.....Z...9.................................................2.....-.8....................-........ 35"4 ...................
12, : 58515 O, 555
TB
TB
.9
. .. . 1-21.7 1A 7 3411 585I-Q714 �Z 7
.. . . 5.3.'.. . . ....... .. ........... .....3.5.1 ....
5T
....... ...... ........ . ......- ........................................... ..... ..
.. ............................ ....... ..............-..................... B
-�901: '98.9 3-64 5.71
360. .55 TB
-------- ------
13:00 12-2.:'�C 169,10: .585"'009:0 3 51 :5,9. .2-6 36, q rz
TB
.................
J A C 6: 56 2.8 358 55 TB
�r4, r, 16:0 9 0 5852 23 33 5-8.
El-
5 TB 1 17,77"0.
::AVERAGE 122.0 17189:: .3.59 5-.9 .2.7 356,
%st.eani:Food:
:83.0
............... ......................... .....................
uf,�,2
............
3 121.7 16880 5852 111.7,::
3 G,1- 5,6-1
35 TB
14 5-4, 122.9 6940. 581-1,21. -32. 3,3 3511 9 6.3 2.6 -5.5-TB
15:-00 123..A;I. .17.110; 5852145-2::Kf 3,.r3;G 5-8. 2.8 35 5-5.*TB
15:15 123.4 17560. 3,69 5.7.
.2-6 351. -5-55 TB
5.55.TB 15,30 123.2 17566 40 .2-:& 3
...........................................
15-:45 1 213-5 17810:: 5852195-5-1 5-3 2.81 358 .5.5 TB
16:.-C* 18,21".10::
5 8 5 2 22,I dri 3,418 2.2: 55 TB
AVERAG 1 3.1 17435 3.53 5.8 2-J: 355 55
84.2.:%sizani,loia-d.
..........
Run 3
ITILDO 12-4.1 '17740: 5852281.1.: 3-3:0 5,34 2-:8 .352.
.5.5 TB
17".1.5. 12*3'..77 .17420::
58523026:: 1.50 5A.: 2.6 365: 5-5 TB
a
17-30 123.7 '18300: 585*12,3155: 3, 53 .2-6 350 5.5.TB
2..& 3:5iu-� 5.5 TB
'219.8 5 10:: 58-5233'.10: -33�-64 5.3'
.......................
1'4� 1.8000u: 5.5 .2-6 3.6-K2. 5.5,
..........
19:15. 124.1 17 5 0, 55LI�5-----663:: 5. -IE5211 .5.5 TB
ANIERAGE .124.0 17833; 5.6 '2..7:: 357 :5-5
%
.................
14

Canfor Southern Pine-Graham Plant
Stack Test Log Sheet
Boiler 4 57,6 MM8tu/hr Rated Heat input
+12AOG Rated Stearn flow
Tct
.....
Steva heswre Stew Row _ 5swwdt�...... _.opac4 Oxygen Trim NiWtidsm Pr re Drop HA i e.2
_...
kifulls
Tanis PSI 8�I� Stara i Comt Stoker 2 COUnt � � MC. VAC kV6C kVtfC
11:30 1154 39214 3MZ45 940734 027 61': 6.1 Z9 3 55 390 55 T8
11A5 16; :2711; 33 6955 8l60926 Oat Cal' 6.1 3A 53' 392. 55 TS
1stA0 123.5a 31254 3946M ''0,°61197 0,26 5.S 6;2 19 393 55 392 55 T'B�_-�»
._.,,_..
12:15 123.3 �#71 S 941371 03€ 60' 6: 3.0 55 391 55 T6
12: 120� Ss 392 Aa1 8 615 031 5�7 6.2 Z9' 35 3 0 55 Tb.
3612v 0A4 53 5.6 Zi 390 55 M9
M 41W 397495 6.0': 6.1 1 393 .55 m 3 55
118E 0.34 59 ._ 55..390 55
96A 5F steam lead
Fang
VMS ".�S'32''. 3�s.MU _ jai!3 0�2 6.C1 Ci.i3 _.._...... ?�`. 366.... 55 34Z 55 Tyr
1M30 7 3 s 3 6 ts3 0,46 5b; 1:4 W S5 390 55 T8
✓
14Z a 3 SM, &:65103
5,8' 6.2 1S t 55 342 55€&
1 � 1.151. 79 391 036371359 6.6 19 3 55 3 55"TB.
t. 1515 114 5, =A7172'. 3 9376 E-"639.'�180 i 6.i� ?.S �3 35._ 35fl _.......55 TB .......... ..
15:30 =- , 1-516 3�9 ,�=16D6.0 TO 3A 392 55 35ti' S5 T5
�,15 t5 123. 404M 39M0 352 6, _6 �` 55 340 S��°AYE3tA�EMo dQm 5.% 65 29 390 55 391 55
5 5+sm m:iwd
16.00 123. 3 3539 133 1:10 6.3'' 6.1 3A 382 5 390 55 TB
15:55' fl?:, 10 S9 0 i 66
3-7 021 5.7 i Y_ 3 g IN
SC 390
55 TS
1'::10 1170 SF61 39`J9'1. 65565 A 61 28 3'W 5 3 55 TS
17,25 W- 37 3451159 8:65?5Y 030 _ 5.8' 5.6 tt 344 55 39A 55'
1'A0' 125.E 1?$16 395135tU0950 042 51: 6.6 IS 30 55 359 5375
I 17.56 119 6 d2. 3951659.; 257 0.57 61 51 30 39A 55 369 55 -0
15:10, 123A 38321, 39517€2' 66381 0,:# 6.i '.v 3.0 FA 55 35t0 55 s3
titSfTSt E 120 Q I L9 2-9 55 389 5S
v ,,...,.,,,»... ..
951 steam Iced
Pin 4
55 TTI
19:15 126 42M M2 301 0,49 ED 34 390 55 ZB
19:30 i2i.3 3E92Cr 39526T6, 4675flf7 050 f 1 fi.6 31 376: 48 3 55 TB
1955 223.7 =151 3g53123 8 67?53 O:# 60. 7At 3.21 3e0b 17 3SU 55'f3
2000 118.3_. 37110 3 3 _ .. U61,934 074 6.1 6.6 32 34 �5 _359 55
20:£6 1b S 3 53512 151 0,35... 3.2 36 53 3 tM
39537k9 8:6839d 0.30 S 9 6.E 3.2 578la119,7 049 6.0
96 d!G oaam load
15

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