EPA 910/9-82-089h
United States
Environmental Protection
Agency
Region 10
1200 Sixth Avenue
Seattle WA 98101
Air & Waste Management Division February 1984
v>EPA Residential Wood
Combustion Study
*
Task 5
Emissions Testing of Wood Stoves
Volumes 3 & 4 (Appendices)
-------
THIS REPORT CONSISTS OF SEVERAL DIFFERENT PARTS.
THEY ARE LISTED BELOW FOR YOUR CONVENIENCE.
EPA 910/9-82-089a Residential Wood Combustion Study
Task 1 - Ambient Air Quality Impact
Analysis
EPA 910/9-82-089b Task 1 - Appendices
EPA 910/9-82-089c Task 2A - Current & Projected Air Quality
Impacts
EPA 910/9-82-089d Task 2B - Household Information Survey
EPA 910/9-82-089e Task 3 - Wood Fuel Use Projection
EPA 910/9-82-089f Task 4 - Technical Analysis of Wood Stoves
EPA 910/9-82-089g Task 5 - Emissions Testing of Wood Stoves
Volumes 1 & 2
EPA 910/9-82-089h Task 5 - Emissions Testing of Wood Stoves
Volumes 3 & 4 (Appendices)
EPA 910/9-82-089i Task 6 - Control Strategy Analysis
EPA 910/9-82-089J Task 7 - Indoor Air Quality
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DISCLAIMER
This report has been reviewed by Region 10, U. S. Environmental
Protection Agency, and approved for publication. . Approval
does not signify that the contents necessarily reflect the
views and policies of the U. S. Environmental Protection Agency,
nor does mention of trade names or commercial products constitute
endorsement or recommendation for use.
-------
RESIDENTIAL WOOD COMBUSTION STUDY
TASK 5
EMISSIONS TESTING OF WOOD STOVES
Volume 3 of 4
-------
TABLE OF CONTENTS
page
APPENDIX A
Nomenclature A-l
Calculations - Sampling Parameters
1. Volume of gas sampled A-3
2. Volume of water vapor . A-3
3- Fraction by volume of water vapor A-4
4. Molecular weight of stack gas, dry basis A-4
5. Molecular weight of stack gas, wet basis A-4
6. Percent excess air A-5
7. Stack gas volumetric flow rate A-5
8. Percent isokinetic A-7
Calculations - Fuel Use
9. Wood moisture, dry basis A-8
10. Wood moisture, wet basis A-8
11. Fuel charge, dry basis A-8
12. Fuel charge, wet basis A-8
13. Wood burned, dry basis A-8
14. Burn rate, wet basis A-9
15. Burn rate, dry basis A-9
Calculations - Emissions
16. Total particulate catch A-10
17. Front half particulate catch A-10
18. Front half catch A-10
19. Particulate matter concentration A-ll
20. Particulate matter concentration A-ll
21. Particulate matter concentration A-ll
22. Particulate matter concentration A-ll
23. Emission factor, dry basis A-ll
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TABLE OF CONTENTS (Cont.)
page
APPENDIX A (Cont.)
Calculations - Total Emission Values for Two Phase Samples
24. Total mass emission rate A-12
25. Emission factor, dry basis A-12
26. Stack gas volumetric flow rate A-12
27. Particulate matter concentration A-12
28. Particulate matter concentration A-12
Calculations - Miscellaneous
29. Front half particulate as percent of total A-13
30. Net efficiency A-13
31. Theoretical creosote deposition A-14
APPENDIX B
Laboratory Results
Oregon Method 7 B-l
Creosote B-4
APPENDIX C
Quality Assurance Data
Wood Moisture• C-l
Particulate Sampling Equipment C-15
Gaseous Measurements C-18
Transmissometer C-23
APPENDIX D
Cost Estimates for Simplified Procedures D-l
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APPENDIX A
Nomenclature and Sample Calculations
-------
Nomenclature
2
An Area of nozzle (ft )
As • Area of the stack (ft2)
Bwo Fraction by volume of water vapor in the gas stream
(dimension! ess)
C Mass emissions factor (g/kg wood)
Cs Concentration of particulate matter in stack gas
(Ib/scf, dry basis)
C's Concentration of particulate matter in stack gas
(gr/scf, dry basis)
C"s Concentration of particulate matter in stack gas
(g/scm, dry basis
Cp Specific heat constant, Btu/mole - *F
Ct Mass emissions (Ib/hr)
E ^ Net efficiency, %
EA Excess air, %
GCV Gross calorific value, Btu/lb
H Heat value, Btu/lb
I Percent of isokinetic sampling, %
M. Molecular weight of stack gas (Ib/lb mole)
Mf, Particulate mass, front half (mg)
M Total particulate mass (mg)
M Fuel moisture (%)
MW Molecular weight
P Barometric pressure (in. Hg)
Dd r
A-l
-------
Nomenclature (Cont.
P Stack pressure (in. Hg)
Q Stack gas volumetric flow (DSCF/hr)
R, Burn rate (Ib/hr, dry)
d
R Burn rate (Ib/hr, wet)
T Meter temperature (*F)
m
T Stack temperature (°F)
t Run time (minutes)
t Sample time (minutes)
V Total volume of gaseous effluent during run
(determined Stoichiometrically) , moles
V Volume of condensed liquid in impingers & silica gel (ml)
3
V Meter volume (ft )
m
V std Volume of gas sample through the dry gas meter
m (std. cond.), ft3
3
V std Volume of water vapor at std. conditions, ft
w
W, . Weight of fuel burned (Ibs, dry)
bd
WL Weight of fuel burned (Ibs, wet)
bw
W, Initial fuel weight (Ibs, dry)
W, End of phase weight (Ibs, wet)
W Initial fuel weight (Ibs, wet)
w
% CO Average percent carbon monoxide measured by NDIR
% C0? Average pe r.':nt carbon dioxide measured by NDIR
% Q Average percent oxygen measured by Oxygen Analyzer
% N? Average percent nitrogen determined by difference
ppm CfiH,« Average parts per million gaseous hydrocarbon measured
b 14 by NDIR, as Hexane
A-2
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Sample Calculations
Example calculations are presented for Run 8.
SAMPLING PARAMETERS
1. Volume of Gas Sampled, standard conditions, (V .)
/ 11 S^.0
/ AH
V . = 17.64 R/In. Hg V /P. +1f1(-
iTi std m bar IJ.D
Uhere
T + 460
m
V = Volume of gas sampled as measured by the dry gas meter
m s (standard conditions), dscf
V = Volume of gas sampled as measured by the dry gas meter, ft (Form 2
T = Average dry gas meter temperature, ~F (Form 2)
m
P, = Barometric pressure at the orifice meter, inches Hg (Form 2)
bar
AH = Average pressure drop across the orifice meter, inches H00 (Form 2)
Y = Gas meter calibration coefficient
Standard Conditions = 68"F, 29.92 in Hg (20"C, 760 nm Hg)
EXAMPLE - RUN 8
29.77 + 0. 314/13. 6
-
v - M7
Vm std ' (17' - 92.61 + 460
= 44.41 dscf
2. Volume of water vapor in the gas sample, standard conditions (Vw st(j»clscf)
V , . = (0.0471 dscf/ml) V.
w std Ic
Where
V, = Total volume of liquid collected in impingers and silica gel, ml (Form 3)
EXAMPLE - RUN 8
Vw std = (°-047i) 75-40 = 3-61 dscf
* Refers to data form from which this value is taken, as indexed in
the appendix; e.g., Form 2 is "Oregon Method 7 Sampling Data".
A-3
-------
3. Fraction by volume of water vapor in the gas stream (B , dimensionless]
* wo
B = w std
wo V + V
vm std vw std
EXAMPLE - RUN 8
B = L10 = 7.52 x 10"2
wo (44.41 + 3.60)
4. Molecular weight of stack gas, dry basis (M, ,lb/lb mole)
M. = 0.28 ( % N, + % CO) + 0.44 (% COj + 0.32 (% Oj
d c i- i-
Where
% CO = Average percent value measured by the NDIR (Form 1)
% CO 2= Average percent value measured by the NDIR (Form 1)
% 0? = Average percent value measured by Orsat for Runs 1-9
2 and by the continuous oxygen meter for Runs 10 - 19. (Form 7)
% N? = Average percent Nitrogen determined by difference. (Form 1)
EXAMPLE - RUN 8
MJ = 0.28 (79.25 + 0.56) + 0.44 (3.12) + 0.32 (17.07)
d
M. = 29.18 Ib/lb mole
d
5. Molecular weight of stack gas, wet basis (M , Ib/lb mole)
M = M, (1 - B ) + 18 B
s d wo wo
EXAMPLE - RUN 8
M = 29.18 (1 - 7.52xlO"2) + 18 (7.52xlO~2)
M = 28.34 Ib/lb mole
A-4
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6. Percent excess air (% EA)
, Eft . :o -icon (1BO)
0.264 (% N ) - (% 02 - % CO/2)
EXAMPLE - RUN 8
_ 17.07 - 0.56/2 _
% EA = 0.264 (79.25) - (17.07 - 0.56/2) (100)
% EA = 406.34
7. Stack gas volumetric flow rate (Q , dscf/hr), dry basis
n - (385 x 60) (V)
~
Where:
V = Total volume of dry gaseous effluent during run
(determined Stoichiometrically) , moles
t = Time of run, minutes
k1 = 385 dscf/mole
k_ = 60 minutes/hr
And V (moles) is determined Stoichiometrially, based on a carbon
balance as follows:
Assume
1. Ratio of dry wood burned to moisture evaporated is constant
and equivalent to wood moisture ratio at start of run.
2. All carbon is accounted for in effluent stream by CO, CO^ •
CgHj., and particulate matter.
3. Carbon content of particulate matter is 70, % mass.
4. Mass content of wood (Douglas fir, dry):
Carbon 52.3%
Hydrogen 6.3%
Oxygen 40.5%
Nitrogen 0.1%
Ash 0.8%
High Heat Value 9050 Btu/lb, dry
A-5
-------
Then
1. Carbon mass, in = Carbon mass, out
2. Calculate mass of dry wood burned, W, ,
3. Establish carbon balance and solve for V, moles
W, , x .523 =
bd
V moles x %C02/100 x 12 Ib C/mole
+ V moles x %CO/100 x 12 Ib C/mole
+ V moles x ppm CgH^/106 x 72 Ib C/mole
+ V moles x 385 ft3/mole x .02832 m3/ft3 x
1 #/454 g x C' g/m3 x 0.7 Ib C/l b particulate
= V/100 C(12 x %C02) + (12 x %CO)
+ (72 x ppm C6 x 10"4) + 1.68 C'D
= v/100 Ck'D
Therefore .523 W. x 100
V moles total = — bd
K1
Where:
'bd
= Weight of fuel burned, dry
W, = Weight of fuel burned, wet
bw
M = Fuel moisture, %
w
V = Total volume of gaseous effluent during run, moles
C1 - Measured particulate.concentration, g/dscm
K1 = Factor = C(12 x %C02) + (12 x %CO) + (72 x ppm Cg x 10"4) + 1.68 C'D
EXAMPLE - RUN 8
0 = (385 x 60) (V)
s t
r
Where V - '523 Wbd x 10°
K1
And k1 = C(12 x %C02) + (12 x ZCO) + (72 x ppm HC x 10"4) + 1.68 C1]
A-6
-------
Then:
K1 = (12 x 3.1) + (12 x 0.6) + (72 x 115 x 10~4) + (1.68 x 0.89)
K1 = 46.72
V = .523 (11.7)(100)
46.72
V = 13.09
Q = (385 x 60)(13.09)
S 155
Q = 1952 dscf/hour
8. Percent isokinetic, (I)
I \v 1 \» W 1 t W
I = 10°
Where
K
Vlc =
V
m
m
P,
bar
AH
Ts =
a =
Vc
s
P
s
An "
l«^WIXll«^-»»«**5\*/ It
Ts (K) (Vlc) +(/) (Pfaar+IfV)
L m
60 a V P An
s . s n
0.00267 in.Hg - Ft3/ml - "R
Total volume of liquid collected in impingers and' silica gel, ml
3
Volume of gas sample through the dry gas meter, ft (Form 2)
Absolute average dry gas meter temperature, °R (Form 2)
Barometric pressure at sampling site, inches Hg. (Form 2)
Average pressure drop across the orifice, inches H^O (Form 2)
Absolute average stack gas temperature, *R (Form 2)
Total sampling time, min. (Form 2)
(F
Stack gas velocity, ft/sec (Calculated from Stoichiometric dscf/hr)
Absolute stack gas pressure, inches Hg (Form 2)
2
Cross-sectional area of nozzle, ft (Form 2)
(Form 3)
EXAMPLE - RUN 8
(100) (295 +460) 1(0.00267) 76.4 + Q, l°'Q'Kn (29.77 +
% I =
p
(0.
(60) (150) (2.39) (29.77) 0.00213
I = 151%
A-7
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FUEL USE
9. Wood moisture, dry basis (M , percent)
Direct measurement with meter or from laboratory sample (Form 9)
EXAMPLE - RUN 8
M, = 126%
d
10. Wood moisture, wet basis (M , percent)
M "
X 100
w 100 + M,
d
EXAMPLE - RUN 8
M = — X 100 M = 56%
w 100 + 126 w
11. Fuel charge, wet basis (W , Ib)
W
Direct measurement from scale (Form 1)
EXAMPLE - RUN 8
W = 38.1 Ibs
w
12. Fuel Charge, dry basis (Wd» Ib)
Wd ='Ww (1 -Mw/100)
EXAMPLE - RUN 8
Wd = 38.1 (1 - 56/100)
W. = 16.8 Ibs
d
13. Wood burned, dry basis (W, ., Ib)
bd
WKJ = W. - W * (1 - MW/100)
bd d f
EXAMPLE - RUN 8
Wbd = 16.8 - 11.6 (1 - 56/100)
Wbd= 11.7 Ib
A-8
-------
14. Burn rate, wet basis (R > Ib/hr)
W - W w
R = W X 60
w
Where r
Wf = Final wood weight, Ib (Form 1)
T = Run time, minutes (Form 1)
EXAMPLE - RUN 8
R = 38.1 - 11.6 X 60
w
155
R = 10.26 Ibs/hr
w
15. Burn rate, dry basis (R. , Ib/hr)*
Rd = ^bd X 6°
*r
EXAMPLE - RUN 8
w * 4.53 Ibs/hr
d
*
NOTE: Final mass of wood is assumed to contain same percent moisture as
fuel moisture at beginning of run.
A-9
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EMISSIONS
16. Total particulate catch (M , mg)
M = M + M,, + M. . + MT , MT , M_
n p ff bf le Iw Ir
Where : (Form 4)
M = Probe and prefilter glassware acetone wash, mg
M = Front filter catch, mg
M,f = Back filter catch, mg
M = Solvent extracted fraction of impinger contents
MT = Water fraction of impinger contents
Iw
MT = Acetone wash of post filter glassware
EXAMPLE - RUN 8
M = 120.9 + 162.3 + 57.1 + 186.8 + 232.7 + 354.6
n
M =. 1114 mg
n
17. Front half particulate catch (M , mg)
EXAMPLE - RUN 8
M = 120.9 + 162.3
Mf = 283 mg
18. Front half catch (FH, percent of total)
Mf
FH = j± X 100
EXAMPLE - RUN 8
283
ffl = U14
FH = 25%
A-10
-------
19. Particulate matter concentration (C's, gr/scf)
M
C1 = (0.0154 gr/mg) (v n )
5 m std
EXAMPLE - RUN 8
C's = (0.0154 gr/mg) (
C1 = 0.386 gr/scf
20. Particulate matter concentration (C Ib/dscf)
fi M s
C = (2.205x10"° lb/mg) v n
5 m std
EXAMPLE - RUN 8
C = 5.53xlO"5 Ib/scf
21. Particulate matter concentration (C11 > g/dscm)
M S
C" = (0.03532 g scf/mg scm) (-n — Q— )
s m std
EXAMPLE - RUN 8
C" = (0.03532)
C1 ' = 0.886 g/dscm
22. Particulate matter emission rate (C., Ib/hr)
Q , T
C. = TT— ^ — X M X 2.205x10"°
t Vm std n
(1H4.25) (2.205xlO~6)
C = 0.107 Ib/hr
23. Emission factor, dry basis (Cf, g/kg wood)
*"
t
r
(]b/hr)(min)
W
hr
60 min
X
bd
EXAMPLE - RUN 8
Cf = (0.107H155) x 15>7 c^ = 23.6 g/kg wood
A-ll
454 g „ Ib 1
lb A .454 kg)
-------
TOTAL EMISSION VALUES FOR TWO PHASE SAMPLES
NOTE that for runs where two phase tests
were conducted, the emission rates for the
combined total test were calculated as
fol lows :
24. Total Mass Emission Rate, Ib/hr, C for combined phases
Where subscripts represent phase 1_, phase 2_, values and total
combined values.
25. Emission Factor, dry basis (C , g/kg wood)
Same as equation #23, with values for total run
26. Stack Gas Volumetric Flow Rate (Q T> dscf/hr)
„ T . (Q. x yltlQs x tr)2
" (Vl + (tr>2
27. Particulate Matter Concentration (C _ Ib/dscf)
c =
28. Particulate Matter Concentration (C11 T, g/dscm)
C
C sj " -^L x (453.6 g/lb) (35.3 dscf/dscm)
JL^X 1.6X104
"sT
A-12
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MISCELLANEOUS
29. Front Half Particulate as percent of total (FH, %)
™= "Vl + "V?
~ (M ) + (M L
n 1 n L
30. Net Efficiency, (£,'%)
Usable Heat Heat Input (HI) - Heat Loss (HL) v
E = = A
Heat Input Heat Input (HI)
Where:
HI = WUJ x GCV
bd
HL = Latent Loss + Sensible Loss
(Latent Loss) =
V {C %CO x MWCO x HCQ x ^ 3 + C ppm HC x MWHC x HH(.10~6D +
C C" x H x 385 ft3/mole x 1 lb/454 g x .02832 m3/ft33}+
C Wu , x 9 Ib H00/lb H x .063 Ib H/lb Fuel + (W. ){M /100)3 Hu
bd c. DW w H
(Sensible Loss)
+ CT - Tn3 {C V x SSCO/100 x C 3 + C V x %C00/100 x C 3
s A PCO 2 PC02
+ CV x % (L/100 x C 3 + CV x ZN-/100 x C 3 +
2 Pn .2 p.,
°2 N2
CWLJ x 9 Ib H,0/lb H x0.063lb H/lb Fuel + (W, )(MW/100)3C }
bd 2 bw pHp
Where:
GCV = 9050 Btu/lb C = 7.0 Btu/mole-T
Prn
MWCO =28 Ib/lb-mole c . 9.3 Btu/mole - T
MWHC = 86 Ib/lb-mole PC02
H = 4350 Btu/lb C = 7.0 Btu/mole - T
HHC = 20966 Btu/lb N2
H = 10,000* Btu/lb C^ = 7.1 Btu/mole - T
P P0^
H, = 1045 Btu/lb 2
H C 0.46 Btu/lb -T
PH2)
* Assume 70% carbon. . .,
-------
EXAMPLE - RUN 8
HI = 11.7 x 9050 = 105,885 Btu
HL = Latent Loss + Sensible Loss
= (Latent Loss)
13.10 {CO.6 x 28 x 4350 x 1/1003 + C115 x 86 x 20966 x 10~63 +
CO.89 x 10,000 x 385 x .02832 x 1/454]} +
C11.7 x 9 x .063 + (26.5)(56/100)3 1045
+ (Sensible Loss)
(295 - 80) {C13.10 x 0.6/100 x 7.03 + C13.10 x 3.1/100 x 9.33 +
C13.10 x 17.1/100 x 7.13 + CIS.10 x 79.3/100 x 7.03 +
C11.7 x 9 X0.063 + (26.5)(56/100)3 0.46}
= (Latent Loss) 37,582 +
(Sensible Loss) 22,108
= 59,690 Btu
Then:
E = HI - HL
x 100
HI
= 105885 - 59690 x 10Q
105885
E = 43.6 %
31. Theoretical Creosote Deposition
1. Assume 15 foot stack with 8 inch diameter; then total
stack surface area:
(15) x (8/12 x 3.14) x (.3048 m/ft) = 2.9 m2
2. Calculate mass of total creosote deposited, CD>
Assuming uniform deposition on total stack surface area:
2 2
Cp.,mg = (mg/m kg)(kg) x m
A-14
-------
3. Calculate total mass emitted, M, mg
M = C lb/hr x t /60 x 454xl03 mg/1b
= C x t x 7.57xl03
t r
4. Calculate percent creosote deposition
Creosote Deposited,% = CQ/M x 100
EXAMPLE - RUN 8
C = 109 mg/m2 kg x 5.3 kg x 2.9 m
= 1675 mg
= 1.7 g creosote
M = 0.11 Ib/hr x 155 x 7.57xl03
3
= 129x10 mg
% deposition = CD/M x 100
= 1675
129x103
Creosote Deposition =1.3%
X 100
A-15
-------
TABLE C-l
Summary of Resul ts:
Wood Moisture Quality Assurance
Moisture Content (Dry Basis)
,a
DATE
6/30
7/07
7/27
8/07
8/13
9/15
SAMPLE
xl
x2
x3
x4
x5
x6
x7
x8
x9
xlO
xll
x!2b
xl3b
LAB
24
24
38
30
19
20
126
105
110
117
40.1
45.1
28.1
METER'
26
27
36
28
18
18
43
c
_c
c
23
25
19
a Eight readings/piece
One cross-section slice only;
all other tests - three cross-section cuts
c Greater than 30, not recorded
C-l
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page 1
'A <
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Wood Moisture Measurement Record
Qua!ity Samples
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Laboratory Results: Wood Moisture
ech laboratory, inc.
2417 S.6. HRUJTHORN6 PORTlflND, Ofl€GON 97214
(503) 233-9871
July 10, 1931
•-li'.'.il Environmental Services
10260 S. '•". Nimbus, M-8
Portland, Oregon 97223
Laboratory Report No. 810713
Subject: Moisture content of firewood, PSOkQ
Sample received: June 30 and July 7> 1981
Sample
5-30-61
X 1-A, 1/6 bark
X 1-BC, fun bark
X 1-D, 5/6 bark
X 2-A, no bark
X 2-3C, 3 A bark
X 2-D, 1/2 bark '
X 3-A, 3 A bark
X 3-BC, 2/3 bark
X 3-D, 3A bark
Moisture
content, %
16,1
23.6
31.7.
Sample
18,
35.
19-6,
37
lil
• 5
• 7
33-3
7-7-81
X ii-A, full bark
X U-BC, 5/6 bark
X U-D, 7/8 bark
X 5-A, 7/8 bark
X 5-SC, 5/6 bark
X 5-D, 3A bark
X 6-A, 1/2 bark
X 6-BC, k/S bark
X 6-D, 7/8 bark
Moisture
content,
30.2
33.2
26.0
17.6
21.1
16.9
19.1*
22.5
16.8-
Test procedures follOTved ASTM D-2016
Moisture content, % c^(A-B)/Bjx 100
Respectfully submitted,
AQUA-TECH LABORATORY, INC.
C. L. Chang, President
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j? °C D/*5
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VF
T-7
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CT-D
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$'7
- x
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CJ t
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,- / : i/ '''
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V
4
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>;
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i> . '
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-------
Particulate Sampling Equipment
-------
..J
tli
r- ' >.f- >*•>
ten* '
o
i
en
" • Enivironmental Services, Inc.
10260 SW Nimbus Avc.. MB
Portland. Ore. 97223
(503) 620-7337
Orlflce^/foV Gas Metet/^fy? Date
n~tti~* ' * r.Ac \;ni IIMC ' ^ I
D
Orifice
lanometer
AH
ln.H20
/SO
Barometric Pressure
GAS VOLUME
Wet Test
Meter
cf
Dry Gas
Meter
Vd.cf
f.007-
^ - Vb (td* wo>
TEMPERATURE
Wet Test
Meter
t ,°F
w
72-
V/
Dry Gas Meter
Inlet
so
a/
fra.
Outlet
e^r-
77
77
Average
SO .?:&S
SO
TIME 1 RESULTS
4
O.mln. y AHg
AHg - 0.03 17. AH
Pb^do* W6»
(t
w
w
Average
ro
-5
cr
-s
QJ
O
Probe Nozzle Date
PI tot Tube
Date
On.ln.
DB.ln.
Dn,«n
Averages
Forward
AP
APstd
C
P
Reverse
AP
AP _
std
C
P
Average
-------
Environmental Services, Inc.
10260 SW Nimbus Ave., M-8
Portland, Ore 97223
(503) 620-7337
CALIBRATION OF "S" TYPE PITOT TUBE
(\)i\rp-
Probe-Type "S" Pi tot Tube: ID. No.
Tubing (ID)
Standard Pitot-Static Tube: ID. No.
Pitot Orifice Size (D)
NBS Standard Pitot-Static Tube C =
0.99
Barometric Pressure
Humidity
Date -
Duct Gas Temperature
Relative
Calibration Operator(s) (=>
x
Legs A, B of
"S" Type
Pitot Tube
A
B
A
B
A
B
A
B
A
B
A
B
A
B
__ - ... 1 — —
Standard Pitot-
Static Tube
AP in. HpO
c.ce
C .07
C-\\
O-C2-
0 • 2H
O.B\
r &i
C TP r t =•
P 1 AF
0,^1
C ,6S"
cnq
c.en
l^C
I.ZC
+ ' ' ~ (
"S" Type
Pitot Tube
AP in. HpO
CM'\
c a\
C - '2.C
C.\S
c .-b(,
o.HG
~l *5
std • r
Lp
Test J s
C-ll
c.^o
v 10
1. 1C
l.&C
i.7e •
- 1 h
Gas
Velocity
ft. /sec.
d
S
Test
Leg A
G.731
O-7JM
o-fece
C-SM1
G . S-39
-
C • *T7
^_- ^ .^ •—
CP
Test
Leg B
0-7^
C-7£7
0.§r'3
C r^l
c . bSi,
•
, ^L,
— ' -
•-
-------
i>
T\ n, r\ n n
Environmental Services
CALIBRATION OF "S" TYPE PITOT TUBE
Probe-Type "S" Pi tot Tube: ID. No.
Standard Pitot-Static Tube: ID. No.
NBS Standard Pitot-Static Tube C = -
Tubing (ID)
Pilot Orifice Size (D)
k 1
0.99
Barometric Pressure
Humidity
Date _
' \ '
Duct Gas Temperature
Relative
Calibration Operator(s)
*J.S '
-^
0
Legs A, B of
"S" Type
Pi tot Tube
A
B
A
B
A
B
'
fl
6
fl
6
£
5
Standard Pitot-
Static Tube
AP in. H20
.0?
.OS
.//
*
. a s
.35-
Cp Test =
~Af
.^
* » ^
. ^7
/. Z
.^
.V^
A/
"S" Type
Pi tot Tube
£P in. HpO
,^7
.
-------
Gaseous Measurements
-------
TABLE C-2
Gaseous Calibrations Data
METER
ORSAT
, Date
7/21/81
7/22/81
7/23/81
8/05/81
8/06/81
Cal
CO
co2
°2
CO
co2
°2
CO
co2
°2
CO
co2
°2
HC
CO
co2
°2
HC
Gas
0.50
7.25
3.57
7.47
Air
0.50
7.25
3.57
7.47
13.0
Air
0.50
7.25
3.57
7.47
13.0
Air
0.50
7.25
3.57
7.47
13.0
3.7
Air
710.
0.50
7.25
3.57
7.47
13.0
3.7
Air
710.
Pretest
0.5
7.25
4.0
7.5
—
--
3.6
7.5
13.0
—
0.5
7.35
3.6
7.5
13.2
—
0.50
7.25
3.6
7.5
13.0
3.9
20.9
705.
0.5
7.1
3.6
7.5
4.0
20.9
700.
Post Test
0.5
4.0
7.5
0.5
7.25
4.0
8.0
3.9
20.8
690.
0.5
7.15
7.5
12.0
4.1
20.5
700.
Pretest Post Test
7.4
3.4
7.5
20.0
0.6
5.0
7.0 ' 6.6
20.6
0.6
•7.0
20.6
0.5
7.0
3.8
20.2
—
C-18
-------
TABLE C-2 (Cont.
METER
ORSAT
Date
8/07/81
8/25/81
8/26/81
8/27/81
Cal
CO
co2
°2
HC
CO
co2
°2
HC
CO
co2
°2
HC
CO
co2
°2
HC
Gas
0.50
7.25
3.57
7.47
3.7
Air
710.
0.50
7.25
3.57
7.47
3.7
Air
710.
0.50
7.25
3.57
7.47
3.7
Air
710.
0.50
7.25
3.57
7.47
3.7
Air
710.
Pretest
0.5
7.3
3.6
7.5
3.95
20.9
700.
0.5
7.2
3.6
7.4
20.2
710.
0.5
7.2
3.6
7.5
4.5
21.0
710.
0.5
7.3
3.6
7.5
21.0
700.
Post Test
0.5
7.1
3.3
7.5
4.0
20.4
700.
0.5
7.2
3.6
7.5
20.5
720.
0.5
7.5
3.6
7.6
20.5
650.
0.55
8.0
3.6
13. Oa
--
650.
Pretest Post Test
0.3
3.2
20.6
--
0.5 0.2
7.4 7.0
21.0 21.0
--
0.5
7.0
21.0
Suspect 13% cal gas used although record indicates 7.47
C-19
-------
TABLE C-2 (Cont.)
METER
ORSAT
Date
9/01/81
9/03/81
9/04/81
9/09/81
Cal.
CO
co2
°2
HC
CO
co2
°2
HC
CO
co2
°2
HC
CO
co2
°2
HC
Gas
0.50
7.25
3.57
7.47
3.7
Air
710.
0.5
7.25
3.57
7.47
13.0
3.7
Air
710.
0.5
7.25
3.57
7.47
13.0
3.7
Air
710.
0.5
7.25
3.57
7.47
13.0
3.7
Air
710.
Pretest
0.5
7.3
3.6
7.5
21.0
700.
0.5
7.2
3.6
7.0
21.0
700.
0.5
7.2
7.5
13.0
21.0
700.
0.5
7.2
7.5
13.0
21.0
710.
Post Test Pretest Post Test
0.5 0.6
7.0
3.6
10.0 7.2
20.0
700.
0.5 -- 0.6a
7.2 3.6 7.2a
3.6
7.5 — 7.0
13.0
21.0 21.0
650.
0.5
7.3 6.4
7.5 7.0
13.0
20.6
700.
0.5
7.0
7.5
—
700.
Switched Orsat before test
C-20
-------
TABLE C-2 (Cont
Date
Cal Gas
METER
Pretest
Post Test
ORSAT
Pretest Post Test
9/15/81
CO
CO,
e.
°2
HC
0.5
7.25
3.57
7.47
13.0
3.7
Air
710.
0.5
7.4
7.5
13'. 0
21.0
710.
0.5
13.0
21.0
660.
0.0
12.8
20.5
C-21
-------
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
Rwrch Triangte Park, North Carolina 27711
,- ..V -ir. :-,, r>.
.*;*„:.. . fl ,,.„ ... ., ^l^L:-. I-ease return,
costs {ji-op.ud, to: 13. 1. ;: v: • -
L-v •'• ' ''':'- ••• i'K'lcct/on Agency
'0;jl'''•''•--"•' -; ''-i"Js Laboratory
lie-search 'J>i:u'g!e Favk, NO 27711
ENVIRONMENTAL MONITORING SYSTEMS LABORATORY
QUALITY ASSURANCE DIVISION
STANDARDS LABORATORY
— /
EJ»A(RTP)420 REVISED 1/80
C- 2 2
-------
Transmissometer
-------
TABLE C-3
Smoke Meter Design and Performance Specifications
Parameter
Performance
Light Source
Spectral response of photocell
Angle of View
Angl e of Projection
Calibration Error
Zero and Span Drift
Response Time
Incandescent lamp operated at ±5% of
nominal rated voltage.
Photopic (daylight spectral response
of the human eye - reference 4.3)..
15* maximum total angle.
15° maximum total angle.
±3% opacity, maximum.
±1% opacity, 30 minutes.
5 seconds, maximum
C-23
-------
FIGURE C-l
Transmissometer Schematic
Photocell:
•Valtec Selenium #R75EB
•Kodak Wratten 103 Filter
Light Source:
•GE 1073 12.8 Volt, 1.80 Amp
Power Source:
•12 Volt Battery (Auto)
C-24
T. N D v 5 1 R I £€
CAPY- A/- C
-------
Emission Test Run
PRETEST CALIBRATION
Transrm'ssometer Calibration (Daily)
Date
Date
Time
7 - /• ( -v,
Operator
cS' 4 S
Calibration Error:
'' .'/ •--•>.'
Filter Value
Zero
Span _
Meter Value
Response Time:
POST TEST CALIBRATION
Date ^
Time /.S"'S"^>
Upscale (seconds)
Operator
Calibration Drift:
Calibration -Error:
Response Time:
Zero
Filter Value
Upscale (seconds)
Photocell: Checked Yes/No
Cleaned Yes/No
Downscale (seconds)
Span
Meter Value
Downscale (seconds)
C-25
-------
^^*^r^^ 1M*
T3
JO
en
r- O.
03
Too
-4-
;t-^
'T"
~
CO
~Q"T-
iz:._±l,
-.- l;--^ j j-
•::.r™' ;i ..o.
• c~J' — -—
:v;»-0-|-,~
s"^="r^j
1 .lU
-^.
—H
- >.. -Ol
^£: -^
-------
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
MOSiro«INC SYSTEMS LABORATORY
TRIANGLE PARK
. NO«TH CAROLINA 77711
CCprtiftrai* nf Analysts
PERCENT OPACITY CERTIFICATION
Filter s True Value (% Opacity)
O3 FH& 007-2.1
METHOD OF FILTER CALIBRATION
The filters were supplied from the vendor with a chart record of optical
density vs wavelength (350 to 700 nm) using a Gary Model 14 spectrophotometer.
These data were verified by using an independent laboratory to check this scan
and their results confirmed the uniform response of the filters over the visible
region. The actual calibration was made using a transmissometer with a well
coTHmated light source and a photopic response. The linearity of this trans-
missometer was checked with optical filters certified by NBS. The values for
each test filter were measured, rotated 90 degrees and measured again. The
average value was calculated in percent opacity and reported as the true value.
SOURCE BRANCH
M. Rodney Mukpett, Chief
c/
C-29
-------
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-------
Transmissometer Calibration
EPA Audit Filters
page 3
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-------
APPENDIX D
Cost Estimates for Simplified Procedures
-------
COST ESTIMATES FOR SIMPLIFIED PROCEDURES
Method
Capital Expenditurec
Item
Cost
Estimated Labor Costs
Per Run
Per Series
(9 tests)
• Total Participate
Sample Unit 5400
Extra glassware 600
Laboratory balance 1000
Platform balance 1000
CO analyzer 3500
C02 analyzer 3500
Q analyzer 3500
Recorder system 1500
Cal ibration gases
9 at $50 450
$20450
If flow measurement system is used instead
of stoichiometric balance then delete:
3 persons x
2.5 days :
$2,100
Then add
Gaseous analyzers, -12450
recorder, and gases
orsat/low velocity + 3000
flow measurement
system
Net difference - 9450
Balance $11000
3 persons x
3.5 weeks :
$14,700
• Filterable
Particulate
Same as Total
Particulate
Subtract 1
mand,ay:
$1,900
Subtract 1.5
manweek:
$12,600
Only major items listed.
at $35.00/hour
Includes time for instrument calibration, laboratory analysis,.data analysis,
and reporting; includes time for additional person to monitor stove if required,
Cost generally less since instrument calibration, data analysis, etc. is spread
out over more runs and time required does not increase proportionally
for number of runs conducted.
-------
Capital Expenditure0
Estimated Labor Costs
Method
Item
High Volume Sampler
CO Analyzer
CCL Analyzer
Op Analyzer
Recorder system
Laboratory balance
Platform balance
Cal ibration gases
9 at $50
Carbon monoxide CO Monitor
C0? Monitor
0 Monitor
Recorder system
Platform balance
Calibration gases
9 at $50
As Screening Method
Orsat
OR
CO/CO Analyzer
Cal ibration gases .
2 at $50
Cost
2000
3500
3500
3500
1500
1000
1000
450
$16450
3500
3500
3500
1500
1000
450
$13450
500
2500
100
Per Run
3 persons x
2.25 days:
$1,900
1 person
2 days:
$ 560
1 person x
1 day:
$ 280
Per Series
(9 tests)
3 persons x
3 weeks:
$12,600
1 person x
3 weeks:
$ 4,200
$600-2,600
Total Hydrocarbon
Same as Carbon
monoxide
Flame ionization
detector
13450
4000-10,000*
$23450
1 person x
2 days:
$ 560
1 person
3 weeks:
$ 4,200
As Screening Method
Orsat OR
CO Analyzer
Flame ionization
detector
Calibration gases
500
2500
4000
200
1 person x
1 day:
$ 280
$700-6700
* High quality heated unit.
D-2
-------
Method
Capital Expenditure
Item
Cost
Estimated Labor Costs'
Per Run
Per Series
(9 tests
Opacity
Opacity meter 500'
Recorder system 500
Calibration filters 50
$1050
1 person x
1 day:
$ 280
1 person
2 weeks :
$2,800
Creosote
Laboratory balance $1000
1 person x
1 day:
$ 280
1 person >,
2 weeks:
$2,800
Smoke Spot
Smoke meter
$ 75
1 person x
1 day:
$ 280
1 person x
2 weeks:
$2,800
D-3
-------
RESIDENTIAL WOOD COMBUSTION STUDY
• TASK 5
EMISSIONS TESTING OF WOOD STOVES
Volume 4 of 4
-------
APPENDIX E
Index
Data forms are presented sequentially by run number and are
indexed within runs as follows:
1. Operating Parameters
2. Oregon Method 7 Sampling Data
3. Oregon Method 7 Sample Recovery Data
4. Laboratory Total Particulate Calculations
5. Flue Gas Exhaust Plume Evaluation
6. Bacharach Smoke Spot
7. Orsat Data
8. Moisture Data
9. Wood Moisture
-------
Operating Parameters
Run H /
Date -7/3.1 !%'' Clock
Stove Name __
Fuel : Initial Cha
Test Charge
Elasped
Time
Minutes
JLff
f&
(tO
72. £>
7<2>
X**} *-
c*^ t Ls
^L~ *\ f~\
Til ')
'/&D
r *•* *** *
in 1,0
Fuel
Weigh
Ibs
t
M
161
ts*
l*\f
/i.<<
/
f
I 3.4
I3.&
n <5
f
1 1.2
n *
ILO
10,1
• /
rge (lb)
Time (24 H)
*•-'• , 7
Operator :^Jl>/ /
Remaining Coal Bed (lb)
pieces lb;
Kindling
f
pieces lb
TEMPERATURES
Combustion
Air
Combustion
Chamber
'
A3
A^T
Mo
1^
//o
tfS
/,o
C02
5,c;
y.5
y-
^^
,^'
^^
v,s~
v,«
V.6
,^-p
Xi
5(o
HC
ppm
^
^^
3^
5^
^/o
^C^)
.^XJ
vi ^^'
3/f
^70
o2?r
300
Opacity
"5O/*
V^%
V^'A-
ID Xo
V^>%
4^ /
wX
3c^
Comments
( Footnotes)
A><;JZ£
Comment Number:
-------
pa
Operating Parameters
Run # / />/Z Date 7/£//&V Clock Time (24 H)
Stove Name
Fuel : Initial Cha
Test Charge
Elasped
Time
Minutes
f/tf
/JLO
126
J30
/3S
Wo
A/<
-D
/ss
j(o o
i 70
Fuel
Weight
Ibs
/P,Y
iO.Q
7,7
7V
K.I
K7
# V
-7 <
1. /
f ^
ft
/ f
rge (Ib)
Rema
pieces Ib;
ining Coal Bed (Ib
Kindling
)
TEMPERATURES
Combustion
Air
Combustion
Chamber
197*
^7°
H7V
472'
/ J..JTV . -
H^b*
^yf
621
£j Cl "J
£-& 2
S37
530
Stove
Surface
c*
M^J&tJ~*^/
3r*l s-^
./ ^tfJ
3/0'
2>ov
3 DO'
,27c>"
*>VD
$/o6
'12o
ljZ>
*>%?>
.^r
Opacity
Meter
Catalyst
,Pre
,
r
\
)
/
Post
/
(
-y
Operator \££> ? /
/
pieces Ib
NDIR
CO
/,/;
te
Ao
^^*i
.7o
,10
M
V?
,
&1S
10
K
,7A
C02
^
*>s
1
HC
ppm
•>00
^0
Ztf
%*t>
.3.™
ASb
3&
326
.2)0
,%%>
560
2(*C
^
Opacity
j6->;.
^.5/1
30?*.
3»l/<
3>#y~
3V 7<
^,x'wX / O
/^j' / / /
, — /'l"c ' rf "
T--.' t/1 ff-illl ^l^-'t/'(
Comment Number:
-------
pa;
Operating Parameters
Run * / Date 7/2 y/X/ Clock
Time (24 H)
Stove Name-
Fuel : Initial Charge (Ib)
Oper
XT" 7
a tor ^--fcr' X /
f
Remaining Coal Bed (lb)
Test Charge pieces ' lb;
Elasped
Time
Minutes
/M
Mb
/?/
tCj "7
30'2
207
2ljL
117
32%
23o
,237
.Z VJZ .
217
Fuel
Weight
Ibs
/ ~ U
O' 7
<.Z
y,?
*/.?
*/. &
1,b
^,H
V,3
1,1
^0
Z.v
3. (s
3,5
Kindling
pieces lb
TEMPERATURES
Combustion
Air
.
Combustion
Chamber
*w
^/^ -
-W3
y/s(,
i
Ao
C02
y?
-To
V/
?V
TP
S~n
*$
?T
i \ <
^ 0
? ;,->'
?^
^
HC
ppm
^0
-7V,
0^,
-7 ^D
,7r
JS&
!*/< •
]l*
1^0
/to
/ S7/
/V)
Opacity
•7 <: ~>
-~\L / -
— f '**•/<_
2(^7'
/27>
) $7o
;of/c
&7o
10%
S0'/j
/U7r
2u7'
^Z0"7.
Comments
( Footnotes)
~_
/^ #/*/''&- f~c
' ' '/•* furn ( ''/"*1
Comment Number:
-------
Operating Parameters
Run # / Date 7/ / /^/ riQr|,
'""" * S f -£*• / / n I V* 1 U I* l\
Stove Name
i
Fuel : Initial Charge (lb)
Time (24 H)
Remaining Coal E
Test Charge pieces lb-
Elasped
Time
Minutes
J5Z
257
26 (
26 7
272
977
el
Fuel
Weight
Ibs
3.3
<^^ y, ^2
Z.I
3,o
3,7
J,^
— ^ ..
Combustion
Air
p=
— — *— — _ _ ^_^
'•' '- - — .—.—
. "•• . — ,
Kindling
TEMPERATURES
Combustion
Chamber
— —
H31 -
137
-+/3-0
^3
Stove
Surface
-•
— " '
£9o*
2*6^
2%o
3-&V
2&Q
33.?
Opacity
Meter
ed (lb)
Catalyst
•>Pre
/
\
V
\
)
/
Post
~
/
\
\
1
^
Oper
f/f-~ '"7
(a tor ^Zr> //
pieces lb
NDIR
CO
r?V
ja
JO
JO
C02
?r<
3*26
^ 1 1*1*
iL
HC
Ppm
S&O _
i7o
\
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2o7c
s~f —
Comments
( Footnotes)
•• ^a^^y
— J-—r 1-S
,-/»_'/,«** /f jSy
_
~"
Comment Number:
-------
Stove Name
Run ti /
Sample Box ft
Probe Length (5 /_
Oregon Method 7 Sampling Data Sheet
W S\J. j
— r—/: :— ^ ' r
Phase I / Clock Time (24 H)
_2 Stack Dimensions
* '
Barometric Pressure
ty- ?6
Probe Material S Nozzle Diameter Q. VOS" *gf
-Cf"-
3>
^frk.t_ ^7
*
<5
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice^AH^
Calc.
•
Act.
Stack
Ts
Gas Meter
T in
T ut
Vac.
Box T
Temperatures
Imp.
WB
DB
Comments
ti
0
/cos
,03*
O
3(0
Jfo
3
-------
pa a- /•
Oregon Method 7 Sampling Data Sheet
Stove Name
Rim #
Date
Phase
Sample Box ti
Probe Length 3,
Probe Material
Clock Time (24 H) /S~QT-
Stack Dimensi-ons o
Barometric Pressure
Train Operators ,Z)d p fc<^«i JlC5
"" ! ' '
-------
Stove Name
Run # I
Oregon Method 7 Sampling Data Sheet
. Date 7/6/Xf/
pa.
Train Operators
Phase # "2-
Clock Time (24 H)
/
Sample Box ft
Rrobe Length
Probe Material
Stack Dimensions
Barometric Pressure
Nozzle Diameter
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
WB
DB
/ CommetA
*
12*13
,0?
36?
7H
755
• cot
262,
e>
-74
77
no
7
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7-
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3-
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09
s.f
2£
no
S
-CP
-Si
so7
,00
'Bl
'35.9
,061
8-7
1 s
76
.061
36
-------
Oregon Method 7 Sampling Data Sheet
Stove Name
Run U ^
Phase #
Date
Sample Box $
Probe Length
Probe Material
Clock Time (24 H)
P-a,
Train Operators
Stack Dimensions _
Barometric Pressure
Nozzle Diameter
-------
Stove Name
Run TT _ /
Box # •
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase if
Clock Times (24 H)
-z//
£"33,;
CONDENSED WATER DETERMINATION
Impinger: #1
Final Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
Front Filter-First Filter t QS~Z
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash
Blank
K
#3
#4
Total
Condensate
-53
r.Q
Back Filter-First Filter #
Back Filter-Second Filter #
CREOSOTE COUPONS
Plate Location
Plate Location
Plate Identification
Plate Identification
Tape
Date
Mg
Date
Mg
Final
Net
-------
Stove Name
Run # /
Box «f
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase #
Clock Times (24 H]
'•5ft-
5-^9-6
CONDENSED WATER DETERMINATION
Impinger: #1
Final Weight
Initial Weight
Net Weight 2. 33
FILTER IDENTIFICATIONS
Front Filter-First Filter # OSS'
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash
Blank
#2
#3
#4
Total
Condensate
M
Back Filter- First Filter #
Back Filter-Second Filter *
CREOSOTE COUPONS
Plate Location
f er
Plate Identification!
Plate Location
Plate Identification
Date
Mg
Date
Mg
Final
Net
-------
0
Stove Name
Run #
Box #
La bo ratory Total Particulate Calculations
Date of Sampling
Date of Analysis
Analyst
Phase 1
L
I.
II.
III
IV.
Rinse & brushings of nozzle, probe, and pre-filter glassware.
Evaporation of_ /ff^ (ml) of^/Zrs^sy? £..
Final '^ ^>? fog) -
- Blank ( (. .'~&H
mg/ml ) ( .
_
*
ml ) =
. mg.) = -2").o'>Lmg s)
Filter catch(es).
Front filter Final o.
/ (mg) - Tare,
+ Back;- up filter Final^./^?^ .fog) - Taret
fog)
Hydrocarbon obtained by solvent extraction of water in
in impingers and bubblers. •-/?
Solvent used />//7 t*L 2, yj-/?*^- . x ,, ^
Final ^. / JgjT ^g ) V Tare ?V. /Tr? (teg ) ^ ^ *
- Blank ( (,co;,< mg/ml ')(_ -^£ ml) =.4i^7> mg) -_
Farticulate from evaporation of water in impinger and
bubblers following extraction.
Final
- Tare
. r '*/u,(mg)
- Blank (( »oiXo mg/ml)( 57»sr- ml total
condensed = \a*& nil) =
T.'T
vi:
Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware.
Solvent used rfss-tj77iL/ /9c
Final b ? y / ? ^ ( a>g : ) - Tar e 4 9. ? »>' fag )
- Blank ('(. g»gpy mg/ml) ('/fp ml) = /.?/ mg) =.
Other particulate catches.
•lotal particulate = I+II-HII+IV-tV+VI
/
mg
mg
Blanks
Acetone Fina
- Tare
Methylene chloride Final 72. *••
= O f ji^ mgX_ y<--> ml = «.t
Water Final 73. ^^n"1 jmg) -
Other Final
mg
( mg ) - Tare_
ml =
mg/ml
Tare
m g/m I
-
(_mg)
mg/ml
- 9 ''?
mg ) x
-------
aboratory Total Particulate Calculations
Date of Sampling 7/?/Xr /
Stove Name .
Run # / Phase # .2, Date of Analysis
Box # 2 Analyst
I. Rinse & brushings of nozzle, probe, and pre-f liter glassware.
Evaporation of, -s^-2- (ml) of_
Final ?/ •'•* < > fog ) -- Tare 7/- J r A./ (mg) >~~t J^&-^ %
- Blank ( ( s.eoi mg/inl)(. ^t?a ml ) = /•*?/% mg ) = 3
me
II. Filter catch(es).
.
Front_f ilter Final o j-^j^ (prg) - Tare o *<£/&_ (jrfg) _£j»g
— - -J 1 - «
III. Hydrocarbon obtained by solvent extraction of water in
in impingers and bubblers. *..t,bef (mg)
- 3lank ((.g.gp
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
(Time 10)
TT/2
-so
£
3A
EC
0
u ^
:C
U
0
O
o
"<- 4
T ime
•35"
35
vr?
. .
-Lv*
35
3,5
!>*?
3O
Stove Name
Date 7/O > / f:
Clock Times (24 H).
Run t !
Phase #
Observer
'_s_
/.-^
Distance to Source
Direction to Source
Wind Direction ,
Wind VelocityQ-^
Cloud Cover ^,
"3O o
No. of Readings
% Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Time
g
1 •-; ^S
1
1
r~
50°
0
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^ .
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Stove Name
Date •' - /- / o .-
Clock Times (24 H) /r^6
Run # /
Phase #
. y
Observer vx ?"},„ /C<:-'>
/
Distance to Source &{O
Direction to Source -^ !^-
Wind Direction U ,^2aJJc~
Wind Velocity (o'— ^
Cloud Cover ,o %
Plume Background £n f " * ^or-^
i>
Stability ^.-v^^ ^
Relative Humidity
/ /*'
Type Contaminant yorfr.'^-}-^ *-•- • ^
w
Color ^.^ 7_ •
'~Lj ^ -— — •Osi'
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
Bacharach Smoke Spot
Run
Date
Operator
Test Time Sample Spot
Number (24 H Elap) Location M' Value
A.
c
JL
3)
8
//r
Test
Number
Time
(24 H Elap)
L//9
-2.
7-3,*-
Sample
Location
S
JL
T
7"
3
-r
S
femp. Spo
Va 1 j
8
--
Comments:
C ^4
-------
Bacharach Smoke Spot
Run
Date 7- ~<- >'•
Operator
Test Time Sample Spot
Number (24 H Elap) Location e p> Value
Test
Number
Time
(24 H Elap)
Sample
Location
emp.
_^
0
H*
21
f/l *
'Z*
/?& r_
<>
s
S/b fcv<
"
P
O -
S
-------
ORSAT DATA
Stove Name
Run # /
Phase #
Date
Operator
Grab Y
Sample Time
Analysis 2
Analysis 3
Average
or integrated sample
&%&$ l%&4- (24 H)
CO
Grab X
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
or integrated sample
(24 H)
C0
CO
>//
Grab
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
CO
or integrated sample
24 H)
Oo
CO
9.
-------
ORSAT DATA
Stove Name
Run # J
Phase #
Date
T /2 I /
Operator "^' C
Grab
Sample Time
Analysis 2
Analysis 3
Average
or integrated sample
(24 H)
co
77
9, /
Grab}( r?& ' or integrated sample
Sample Time /TO / (24 H)
Analysis 1
Analysis 2
Analysis 3
Average
CO
S.4
Grab
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
or integrated sample
(24 H)
C0
2
CO
4,2
/. ^
M.£
I2J-
-------
ORSAT DATA
Stove Name
Run ;?
Phased
2.
Date
Operator
-"!' 0. ., ( 1 r.
Grab
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
or integrated sample
; (24 H)
co
CO
TI4
Grab
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
or integrated sample
II4O (24 H)
co
C0
Grab
Sample Time
Analysis 1
Analysis 2
Analysis 3
Average
or integrated sample
[ (24 H)
co
-lo.c
A.
'0,0
-------
OR5AT DATA
Stove Name _
Run T? 1
Phase #
_ Date
Operator
iL /!
-------
Moisture Data
Stove Name
Run # _Z
Phase
Date
Operator
i /TV
Time (24 H)
Temperature
Wet Bulb Dry Bulb
Moisture
Percent
r
-------
Wood Moisture
Date "7/27 / W
Operator
Test Run #
1
Meter Measurement
FUEL
2
3
4
5
6
8
9
10
11
12
A [ B
13
ll
24
a. 4
a?
24
/7
24
-If
Percent Moisture
Total Mass (Dry Basis,
JU
AVE
-
57
-------
pa i
Run
Date
Operating Parameters
Clock Time (24 H)
Operator
Stove Name
Fuel: Initial Charge (Ib)
//
Test Charge ^7, H Ik pieces fa
Remaining Coal Bed (Ib) £t0
Ib; Kindling /. 7 /{,*> pieces _^
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Opacity
Meter
Catalyst
Pre Post
NDIR
CO
C0
HC
ppm
Opacity
Comments
( Footnotes)
/D
I
'0
312.
32.1
••}>7
t.j'jj
r H e/'
&L
f/o
15. 1
I, I
_J
Comment Number:
-ft
^^X^- /-
-civ-i tc-^-n
-------
Operating Parameters
Run § P_ Date 7/tl /#"/ Clock
Time (24 H)
Stove Name >'„
Fuel: Initial Charge (lb)
Remaining Coal
Test Charge pieces lb;
Elasped
Time
Minutes
66-
7/7
7£
C^"7~1
Q ^
X£
97)
?S~
/#£>
/df
I/O
/JD
/<£<
Fuel
Weight
Ibs
/vY
/3,<7
a 2-
L>e2.7
y^3
/A 7
//. 3
/A^
/5J
f . y
^^
?,^x
a»
Kindl ing
Bed (lb)
TEMPERATURES
Combustion
Air
Combustion
Chamber
J3/
51 JL -
s/o
^o
MS
£>V\
JJf
53r?
J^y?
52 H
C ncs
uJsO
Sil
Stove
Surface
/j 7T)
L! So
i$8
L\HV
Lftf
*~4*~)O
WD
tj ^.^
^$0
Wd
V3&
HSO
^70
Opacity
Meter
Catalyst.
-.Pre
/
\
\
/
/
(
\
i
'
Post
r
\
\
I
I
\
\
\
Oper
a tor vc'V- f/V
pieces lb
NDIR
CO
A*
1 *>
IV
/ ^
),tf
/v
/>
ft
Ao
C02
^
7r,
/ 5"
7<^
7<
•70
7^
7/r,
/^.<
6,0
7.^
>y(0
.V,
HC
ppm
*JOft_
Wfi
Wp
ye/?
'5C0
ty-So
Kl)
Hri
^\5^
$75
W
,W
Opacity
^f,
O'J-^
6M
/ r7v
bo?o
f«o70
6?t>7>
70 K
?da/o
70%
frS*7)
667*
•
Comments
(Footnotes)
^fr^-i/j^
•3 .'A') *
fife*/ / L '/a fttfrt &J
/W, / (J
•
Comment Number:
-------
pa a>_ ^^ ^ i
Operating Parameters
Run # c2^ Date 7/^L2Vo ( Clock Time (24 H)
Operator y.V • 1
/ /
Stove Name
Fuel : Initial Cha
Test Charge
Elasped
Time
Minutes
id &
/36
MD
i*f5
)*r
JbD
I-7T)
/?<
/S7?
/ * 1 1 _/ —
MO
Fuel
Weight
Ibs
li^
7,1
Ss,< D
£^
£>Z~
L\ Ol
V.&
/J U
*/,«.
rge (Ib)
Remaining Coal Bed (Ib)
pieces Ib;
Kindl ing
pieces Ib
TEMPERATURES
Combustion
Air
Combustion
Chamber
.
-------
pa3-
Operating Parameters
•, i-
'9
Run ti J/^ Date 7/21/tf'/ Clock
'XX
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
Elasped
Time
Minutes
itf-S'
$00
J^~
310
(*J y £-^*~*
V^- * L^
5^0
j^-r
3— ~7
z.
2Y0
^y^-
2^2?
9 r4/
A- *«^-/" — -—
Fuel
Weight
Ibs
Lft 1
3.?
3.r
3,7
3 10
o *^
53
S,Z
^2,9
?, ^
^^^- i j&
o ^^
Time (24 H)
/ <#'>
^
Operator ^-~,^
--> .••'">
~- t' /
-* x /
/
Remaining Coal Bed Ib)
pieces Ib;
Kindl ing
pieces Ib
TEMPERATURES
Combustion
Air
Combustion
Chamber
5/9
t_x ^^- /
CX / 0
JT/3
,-^c|
.5^2.^
^L^
S^o
S^/7
£Hl
Stove
Surface
?00
Vflfl
.^90
3^
^yo
3^
,570
37£
^7o
,5 cT^
? c^n
\ rS ^/
* 0^*V\
Opacity
Meter
Catalyst
-.Pre
(
\
\
/
i
i
\
\
^^-^^
Post
/
\
1
/
/
t
i
\
\
1
\
NDIR
CO
,&
^
SV
3*
£*
M
D
J-o
HC
ppm
/ ^S
M
/&&
Jio
}&
125
/ao
MD
//o
JCO
Opacity
7 L^1
%)%>
VM
33 ?o
3&7o
*>S7o
35%
•$Q%>
< ^7-
. )c-/n
J>5'X
C^»-^ ^_*
>0 \'
Comments
( Footnotes)
•
ty^>' fr/~
&t *>;,•?,„.>,
if,Ju+ <>--> ]
Comment Number:
-------
Oregon Method 7 Sampling Data Sheet
Stove Name
Run
-< .
Barometric Pressure
Nozzle Diameter
•. klA\S^~^
Elasped
Time
Meter
Vol
Pi
AP
Orifice AH
Calc.
Act.
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
MB
DB
Comments
,49
c
D
,61
O
7?
•00^
5V. /3
O
361
37
Sz
O
n
7.T
3D
'^(53
_Q_
r±
003
.to
0
. fO
73
15X351
u
M-nf
^
&
^±?
-------
Oregon Method 7 Sampling Data Sheet
Stove Name _
Run t Z,
H0
Date
Phase
Sample Box #
Probe Length
Probe Material (^
Clock Time (24 H)
Train Operators
Stack Dimensions _
Barometric Pressure
Nozzle Diameter
:— \7(
-------
^r
r" 0
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J*>
pa.
Qrkgon Method 7 Sampling Data Sheet
Stove Name
Run 9 2.
H@
Date
7/7^/5*1 Train Operators P^/O
Phase 1
Clock Time (24 H)
Sample Box # <^-
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
Nozzle Diameter
-------
Stove Name
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase
Box e
CONDENSED WATER DETERMINATION
Impinger:
Final Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
#1
//
.IT
Front Filter-First Filter #
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash
Blank
Plate Identification
Clock Times (24 H)
#2
#4
A 7
O.I
Back Filter- First Filter #
Back Filter-Second Filter #
CREOSOTE COUPONS^
Plate Location
Plate Identification
2
Total
Condensate
Tape
Date
Mg
Final
Net
Date
Mg
-------
Stove Name
Run •?
Box r?
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase #
CONDENSED WATER DETERMINATION
Jmpinger: #1
Final Weight
Initial Weight
Net Weight /?•£
FILTER IDENTIFICATIONS
Front _FiHer-First Filter #
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash
Blank
CREOSOTE COUPONS
Plate Location
Plate Identification
777"
Clock Times (24 H)
#2
#3
£37.0
/3
V.2V.7
7J/.V
Back Filter-First Filter #
Back Filter-Second Filter #
Plate Lo'cation
7/2
Total
Condensate
Plate Identification
Tape
Date
Mg
Final
Net
Date
Mg
-------
Stove Name
.aboratory Total Partlculate Calculations
Date of Sampling 7/21/J' /
Run # ^J2_ Phase # / Date of Analysis
Box * / - Analyst
I. Rinse & brushings of nozzle, probe, and pre-fiiter glassware.
Evaporation of. *=•*- .(ml) of
Final ?**^JB»' (rag) -
'
_
- Blank ((.-.gfr? mg/ml)(. /T7 ml ) = A?3 mg )' =
II. Filter catch (es). pf 2^7/r_ P.f
_ .
Final.o.w.r.Crog) - Tare.fl. ^^V (mg) ^^ ?/
filter Final g.^agjmg) - Tare^o. »6^9 (mg) =g'>xs6>i^ mg
£7. U-ctfC? ^
III. Hydrocarbon obtained by solvent extraction of water in"
in impingers and bubblers. ,-
Solvent used ^//Z ^Z. 2. JHr— A
Final 7
-------
Laboratory Total Particulate Calculations
Date of Sampling
Run # X__ Phase # 2^- Date of Analysis
Stove Name . . ,
•*"> ^7
x p U •* p Q •»* >X"^
Box f? 2- Analyst
I. Rinse &. brushings of nozzle, probe, and pre-filter glassware
Evaporation o£_ s->/ (ml) of_ /r^s-/^ -^ — •- ^
Final •? / :-rv/ (mg) - Tare 7 /'••?> 3- 7 Cipg) 5 : ?. ' '"'^
- Blank ( (. ,g?o3 mg/ml ) ( . "J2\ I ml ) = 8.\3W mg ) = 3l7.
II. Filter catch(es). _ _
- Tare o. ^/ ^-r °- J ' '
.,
i +/3ack-up filter /Final g >-^7:^ (mg) - Tare, o * k b~) tCyg ) = t^«-r ^V, -' "
- Blank ((_.gfc?6 mgml)( 2 ml total
ml condensed =.J££j__ml) = U^ mg)
^ 1.3
V. Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware .
Solvent used _ //ts-/an^
Final 7A 'ft (mg) - Tare 7«y. y^yj (\ng)
- 3lank ((_.&?pg ) "*jz-^ '?/•* tf-
- 31ank( ( .ovZf mg/mlH yjf ml) = . c^aQTrng) =. /^.Tf mg
VI. Other particulate catches. =A _ mg
VII. iotal particulate = I+IH-IIH-IV+V+VI -f
,
Blanks
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
.,_7, ^ ^„ t-io
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: ., , . Stove Name
Date - ' ,^ ,;• / -C -'
Clock Times (24 H) /3 xr,^-,
, ' Run # -ty ^
•|?ki Phase i
Observer ^ ^j>^ /L&a
Distance to Source 2S ^-^L^J~
Direction to Source -S zL_
Wind Direction S OO - ^^1-*. , & /} hi
Wind Velocity O-'*L<~" ^>/?^
/
Cloud Cover 3O ^
Plume Background T^-^r^/'A
Stability x<>v-c^/' A->-> ',«?-•
Color ^XZ*J7>
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
I f
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Stove Name
Date
Clock Times (24 H)
Run I ggr
Phase #
,' '•//.'*)
Observer
Distance to Source
Direction to Source
Wind Direction ^
Wind Velocity £
Cloud Cover ^
-
Plume Background
Stability _-,,
Relative Humidity
Type Contaminant /,/,;-
Color ' /, ^-L^-<^r
ru D
No. of Readings
% Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
iTime
1 - ~,
'
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\
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Clock Times (24 H) ;2 ^T
Run # /^--4>
Color .,v^,,^
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
(Time
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Type Contaminant ^.r^T*^' ^o^>^e«-^!
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'0
No. of Readings % Opacity
0
10
20
30
40
50
60
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Minutes of Observation
-------
Bacharach Smoke Spot
Run #'oJ Date 7/V -- Operator
Test Time Sample Spot Test Time Sample Temp. -
Number (24 K Elap) Location emp' Value' Number (24 H Elap) Location Vc
t-
^ 7
3_ MT
Co- I&.7
•ZL
Comments:
• Jt
.£.
-------
ORSAT DATA
Stove Name
Run #
Date
Phase H
.1 9f-
Operator
Sample Time { 1L 1 I
C02 02 CO N2
Accumulative £ ^ ,~ >• Q^.9
Net J/X g^ 1.4 7f.V
Sample Time
Accumulate
Net
co2 o2 co NZ
Sample-Time /4 3O
co
CO N
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
.4".
•-£"
co
CO N
co
CO
-------
ORSAT DATA
Stove Name Date /
C02 02 CO N
Run # Q _ Phase # ^L, Operator
Sample- Time
Accumulative
Net
Sample Time
, C? 4
Accumulate 5". £
Net I. I,
Sample -Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
C02 02 CO
C02 02 CO
C02 02 CO
C02 02 CO
-------
Moisture Data
Stove Name
Run # Q^
Phase #
Date
Operator
Time (24 H)
Temperature
Wet Bulb Dry Bulb
.3><<0
144
/lo 2-72.
114
\\0
Moisture
Percent
/7
4
-------
Date
;/2;>
Operator
Wood Moisture
Test Run #
2
FUEL ff
1 4
3
4
5
6
7-
8
9
10
11
12
Kindling
Total Mass
13.
11-0
cu
Percent Moisture
/£'
i.r
Meter Measurement
Total Mass (Dry Basis)
\4S
K/.o
4
IS.e
1S-T
no
/.I
(2.0
//.
AVE
}4
I*/
-------
Run I
Date
Operating Parameters
Clock Time (24 H) /
Operator
Stove Name
Fuel: Initial Charge
7,^" Test Charge
pieces
Remaining Coal Bed (lb)
lb; Kindling cSf,i'-&•
.10
1
yo
/ ,- i?7
h /*
n
'AD
,*>
i ^OJ
hi*
Comment Number:
/. I
-------
pa.
Run
Date
Operating Parameters
Clock Time (24 H)
Operator
/ /
Stove Name
Fuel: Initial Charge (Ib)
Test Charge pieces
Remaining Coal Bed (Ib)
lb; Kindling pieces
Ib
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Opacity
Meter
Catalyst
Pre Post
NDIR
CO
C0
HC
ppm
Opacity
Comments
( Footnotes)
70
m
'
7P
io
3
5 <*7
3,0
/Jo
ID
3.
o
7 -
IM.
l£j-
}dS
/oD
•ft ) JtA,'^: (J/'ftJ
.'
,6V
O&.
<
\
\
'07
r-o 3/<-/ fyu'r
"I bit
Comment Number:
l^l\h u ^ —
-------
pa3- _ts
Operatinq Parameters
Run 1 .^> Date 7/Z 3/C / Clock Time (24 H)
Operator ^. 3 ,J" •'
Stove Name
Fuel : Initial Cha
Test Charge
\
Elasped
Time
•linutes
f^S\^iS
1 fJ i \
/^
i£o
I&T)
/7z>
t7<^
iKO
)X^
Mb
Fuel
Weight
Ibs
*, 7
7, ft
?.*>
ft. (?
/ /
10. i
*),ls
5V
H tf
rge (Ib)
Remaining Coal
pieces Ib;
Kindl ing
Bed (Ib)
pieces Ib
TEMPERATURES
Combustion
Air
Combustion
Chamber
7ob
/^5Z -
73(^
65Z)
6/V
— ^-^/ * * —
^tf
520
571
7hZ
Stove
Surface
42^
LJ3D
HIO
Hn®
Hoo
s~
«O 0^>
^> &0
?&
^&
\^V
^^0
Opacity
Meter
'
Catalyst
.Pre
1
i
1
i
i
1
Post
/'
I
I 1
\
1
\
\
\
NDIR
CO
uC
iO
96o
£b
Sp
,100
,7d
,-70
W
C02
M
U
W
1,0
1M
iv
V
3,2,
W
M
HC
ppm
I/V
&)
^5-
nZ5"
ao
i^T
/60
^2-/0
^^
an
/^r
Opacity
/, )/j
/ J -'
/^%
)%7o
/g-%
W%
M
K%
j£?~
/ 57,,
Comments
( Footnotes)
^Z ™veo/^ '*
f.n* JJ-'K<~ -
\ i V". /
Comment Number:
-------
Stove Name _
Run # .3>
Oregon Method 7 Sampling Data Sheet
A £? _________ Date rZQj?//?/
Train Operators _
Phase #
/
Clock Time (24 H)
Sample Box #
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
>'U * "
t'< Q
Nozzle Diameter
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
WB
DB
Comments
0
£-7
0
367
S-s-
87
o
y
H
10
87
70
t,
2S-0
69
30
8-7
6
6?
366
0(33
.z-S
310
13.
307
S7
3o
3>
o
'00
.1?
0
3o^
O
6?
.-31.
.6
^30
-------
Oregon Method 7 Sampling Data Sheet
Stove Name _
Run i B>
m
Phase i
Dgte
Sample Box #
Probe Length
Probe Material
Clock Time (24 H)
Train Operators _^>"t--1
Stack Dimensions
Barometric Pressure
Nozzle Diameter
-------
tor}
Oregon Method 7 Sampling Data Sheet
Stove Name
Run #
Sample Box #
Probe Length
Probe Material
-------
CT^iSji" Environmental Services
1380 NW Lancashire Ct.
Beaverton. OR 97006
(503) 645-9685
D
SOURCE SAMPLING-LABORATORY ANALYSIS OF PARTICIPATE SAMPLE
T«t £
Date of Test
..3 .Pft /
Project #
7/2.
CONDENSED WATER DETERMINATION
Impinger:
Final weight
Initial weight
Net weight
#1
^-5^.<^
.TWJ. *>
$2
£>-//. 3
-rj^.y
_r.T.3 •: 4.1
?3
y^r.v
^27.^
o.f
#4
773,*S
7&9.J.
4. a
Total
Condensate
/^
FILTER IDENTIFICATIONS
Front Filter-First Filter
Front Filter-Second
QT^^-^NFORMATION, COMMENTS
Back Filter-First
Back Filter-Second Filter#
ORSAT DATA
CO,
Analysis 1
Analysis 2
Analysis 3
Average
CO
CO
CO
N,
N
22 "2
Atomic Wt. Atomic Wt. Atomic Wt. Atomic Wt.
(32) (28) (28)
Time
Test conditions:
-------
Enivironmental Services, Inc.
10260 SW Nimbus Ave., M-8
Portland. Ore. 97223
(503) 620-7337
LABORATORY TOTAL .PARTICIPATE CALCULATIONS
Source Description,
Plant - Date(s, ^
Sampling Date(s). ?/12>/gri Run # J> ftf / Project # ^5'cPVy
I. Rinse & brushings of nozzle, probe, and pre-filter glassware
Evaporation of. **•? (ml) of
(rag)
,
- Blank ( (. .£?£*? mg/ml ) ( . a2 T . ml ) = g-<9* T mg ) = ^£7.67 mg
II. Filter catch(es). F
Front filter Final.g.r$yg .(mg) - Tare^-v737 J^g)
•+• Back-up filter Final p. .^9-^ (mg) - TareTg./.f-/7 ^mg) -
III. Hydrocarbon obtained by solvent extraction of water in
in impingers and bubblers. ff
Solvent used GHJ.&t-^' JXT'~< ^
Final ?V. 7<:r6 (Hg ) - Tare ?^. s-Tgf C>Qg ) '***' f ^¥' 7 "^
- Blank U >c?oqr mg/mij.L irj^* ml) = ..2.<3.r mg) =.IW.4t mg
IV. Particulate from evaporation of water in impinger and
bubblers following extraction.
Final 7r.
- Blank ( (
V. Particulate from solvent rinse of impinger, bubblers,
and post-filter.glassware. -
Solvent used X?^rr4^ ^ a./
-------
Enivironmental Services, Inc.
10260 SW Nimbus Ave.. M-8
Portland. Ore 97223
(503) 620-733?
LABORATORY TOTAL -PARTICIPATE CALCULATIONS
client Source
Plant . Date ( s ; Analysis.
Sampling Date ( s ). 7/2?/X/_ Run 3 ?0M2^ Project #
I. Rinse & brushings of nozzle, probe, and pre-filter glassware.
Evaporation o£L ftf (ml)
Final 7ff.^if (mg) - Tare "7 »"•*.» fej (ipg) ?W~ 9 •*--<+
- Blank ((.. .00? me/ml )(. TJT .ml) = g.7£.r mg) = ?4. £4 mg
II. Filter catch(es).
Front filter . Finals .*--e--c
IV. Particulate from evaporation of water in impinger and
bubblers following extraction.
- Blank (i -•£ .gg>^ mg/ml ) ( 2*^O ml total
- Ty
V. Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware.
Solvent used /
(mg) - Tare 73.j- ml) = gL>Q34 mg) =,
Acetone Final
Me thy
Water
Other
s
lene chlori<
—
Final
=
Final
—
(mg)
mg/
3e Final
mg/
r(mg) -
mg/
(mg) -
mg/
- Tare
ml =
(mg)
ml =
Tare
ml =
Tare
mj. =.
(mg)
mg/ml
- Tare
mg/ml
(mg)
mg/ml
(mg)
jng/mi
- Blank ((. too2^"mg/mi)(, rr ml) = . g?J&LSmg ) =.111^? mg
Final. 7j.g*?6 tmgJ - Tare "7^. ;^7(»g) ^^-^ 7^ mg/ml ) ( 2*^O ml total
ml condensed =.\&& ml) = jJ-gS'mg) » 7S>7y mg
J
VI. Other particulate catches. =, — mg
VII. Total particulate = I+II+II1+IV+V+VI
Blanks
(mg)
-------
Bacharach Smoke Spot
Run ^ Date 7/ Operator
Test Time Sample Spot Test Time Sample Temp. Spo1
number (24 H Elap) Location p> Value' Number (24 H Elap) Location Value
^_
Oi 1124 O jTQ („
-S 2M JL.
-A. 32£> 9
\°rlO O 2SC? 7-
X7 MM- o S3J" (^
2T
Comments;
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Stove Name
Date
Clock Times (24 H)
Run # 3
Phase #
Observer
Distance to Source
Direction to Source
Wind Direction _/
Wind Velocity
Cloud Cover
-S F
O -jf
Plume Background
Stability ..-.••,
Relative Humidity
Type Contaminant
Color
No. of Readings
% Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
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Stove Name
Date
Clock Times (24 H)
Run #
Phase I .^_
Observer " "2~ /' r
/ ,_;
Distance to Source "<,:V
Direction to Source L r
Wind Direction _7r^xr^r
Wind Velocity •" - 5
Cloud Cover • '-tC^f^SC^o
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Relative Humidity
/
Type Con tami nan t •,/ ->>-_-vjrV; " ^. -r>-^ ;
Color :<,.- ',./ -<,^
No. of Readings % Opacity
0
10
20
30
/in
M-U
50
60
r o _,
OU+
Units No.
Minutes of Observation
-------
ORSAT DATA
Stove Name Date
7/2
'/ ~~T~ n>
Phase # J- Operator A L-
Sample Time /2.4-4-
C02 02 CO N
Accumulative
N" I/. 7
Sample Time
co2 o2 co
co2 o2 co
Accumulate
Net
Sample Time
Accumulate
C02 02 CO N2
Net 3,-£ /6.3
Accumulate ^>°< J^jJ 3oA
Net -i» 2 /% O ^?r C> /?. £ -SC^^. T 10
Sample -Time I ^> ]»S
Tims
Accumulate _c
Net (.3.
co2 o2 co
-------
ORSAT DATA
Stove Name _ ^ _ Date ~7/ 2.~* / ? (
Run # ~> _ Phase $ ,'/L Operator ^- _
Sample Time I 4 -S j
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
C02 °z co
Accumulative
Net
Sample Time j _
CO. Oo CO
C02 02 CO
C02 02 CO
C02 02 CO
-------
Moisture Data
Stove Name
*~
Run #
Phase #
Date - "*>
?"/
^X Operator
Time (24 H)
I4S&
Temperature
Wet Bulb Dry Bulb
ISO
ISo
Moisture
Percent
j£
it
ii
-------
paa.
Run
Date
Stove Name
Operating Parameters-
Clock Time (24 H) ^ ^tS*?
J^T '#
. 7
Fuel: initial Charge (lb) ,£
-------
Oregon Method 7 Sampling Data Sheet
Stove Name
Run #
Date
Train Operators
Phase
Sample Box # /^/J-yso «*^// Stack Dimensions
Probe Length
Probe Material
Barometric Pressure
Nozzle Diameter
Clock Time (24 H) O9$'9- /03^
€^ fi S~T{
O &J
G0 - O, $03
7
£L
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac
Temperatures
Imp.
WB
DB
7
. .
Comments
o
40
M5"
"70 /
o
-772^
7
00^
0
• o/o
•50
76
o
5.66
iZ
\?
^^
293,
31
c
^^
-------
Environmental Services
K;SJ NVv Lancashire Ct
Eesverton, OR 97005
,5.03' 645-S6S5
Test
SOURCE SAMPLING-LABORATORY ANALYSIS OF PARTICIPATE SAMPLE
Project #
Date of Test
CONDENSED WATER DETERMINATION
Impinger:
Final weiqht
Initial weight
Net weioht
Fl
."T&y, ^
-f*i3^f ^
$2
5~3<3, ^
•S\$(0. t
3& • C * "\.*i
?3
*/2$~. 7
4t2'7. *?
f> . *%
#4
&J!T.Jf
7&&. 7
I. 2
Total
Condensate
..
^- ^ .%" <^
V. _^
FILTER IDENTIFICATIONS
Front Filter-First Filter #«
Front Filter-Second Filter JL
OTHER INFORMATION, COMMENTS
Back Filter-First Filter^
Back Filter-Second Filter#
ORSAT DATA
CO,
Analysis 1
Analysis 2
Analysis 3
Average
CO
Time
Test conditions:
CO
CO
N
2 2 2
Atomic Wt. Atomic Wt. Atomic Wt. Atomic
(32) (28) (28)
-------
Enivironmental Services, Inc.
1026C SW Nimbus Ave . M-8
Pc.'i.and Ore 97222
LABORATORY TOTAL -PARTICIPATE CALCULATIONS
? & As
j-iar.t
Sampling Date(s). g^-^
I.
Source Description^
Date(s) Analysis, .; - >" -
Run # ' ^/ Project
II
III
IV,
VI.
vi:
Rinse j/*^ S 3^ -.
&r. < .
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Time
ii/3 0
Wl?
/O[i-
- — ! —
fOf^
l
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—^2 —
^?C7
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Stove Name
/ ~-/
Date ?5/f?Ar/
rinrk Times f24 H) O (O/Z>
t
Run # ^-T
Phase # (^r-C/^u^x-T
/o
Observer Y&(
,
Distance to Source S&f-A
pirprtinn to Source /JlAJ
. . _.
Wind Direction -^-^ A/^
Wind Velocity (O- 2 —
^
Cloud Cover /O/o
_/ ._-
Plume Backqround Z<^-fra-
Stabilitv
Relative Humidity
Tvpe Contaminant
x/ ~^~
Color £o"AxxC£>
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
Run
V
Bacharach Smoke Spot
7 Date /
Operator
Test Time Sample Spot
Number (24 H Elap) Location H- Value
iotf
Test Time Sample Temp. -
Number (24 H Elap) Location Ve
II
Comments:
-------
ORSAT DATA
Stove Name _ Date t / s / C /
Run # T _ Phase # _ Operator ""^ . C_
Sample Time -yiip-eHf ^10 \ "^.
CO
Accumulative
--j -o &
Net
Sample -Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time /£ g
C0 0 CO
Accumulate f .11 \l-4- 2q
Net T-?
C02 02 CO
C02 02 CO
C02 02 CO
-------
Moisture Data
•Stove Name Date 6 /
Phase $ ~ Operator "-/
Time (24 H) Temperature Moisture
Wet Bulb Dry Bulb Percent
-------
Wood Moisture
Date '2 / C / ~6' I Test Run # 4
Operator "A,. C3
Meter Measurement
FUEL
1 4^
3
4 ^
5 rr
5. C fc
-*
/rv
8 ^
9 -^*
10 ^
11
12
Kindling
A
11
,Q
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a
K-
;i
H-J
^
B
|pX
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//.^
l.?.T
li.l
Q.*
IS. t
/i.^
/M
!S.^
^7
a^r
Total Mass (Dry Basis)
-------
Run a Q W Date
Stove Name
Fuel : Initial Charge (Ib)
Test Charge / pieces
Operating Parameters
Clock Time (24 H)
Operator
c ~' /
Remaining Coal Bed (Ib)
Ib; Kindling pieces
Ib
El asped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Catalyst
,Pre
Post
NOIR
CO
C02
HC
ppm
Opacity
Comments
(Footnotes)
D
S
37,0
JL
7s
/o
732-
.X
£0
So 7
(o.O
so
70
Z2
lU.b
Comment Number:
SZI
ho
r
o
\to V V-
-------
Run I
Date
Stove Name
Operating Parameters
Clock Time (24 H)
Operator
Fuel : Initial Charge (lb)
Test Charge
pieces
Remaining Coal Bed (lb)
lb; Kindling
Elasped
Time
Minutes
Comments
(Footnotes)
/r r f
I .j *->*•*-'
Comment Number:
-------
Operating Parameters
Run tl ,-"S Date £r^£T' o / Clock
Time (24 H)
Operator
Stove Name
Fuel : Initial Cha
Test Charge
Elasped
Time
Minutes
/3d
)3
/So
^
/ { ) ^
/too
!*,<
fin
/ 7S
/ xo
ftf£
/?$
Fuel
W-eight
Ibs
#,£
gr;y
27
7.6
ZV
7,2
7^.
K^. O
M, /
/i-2.
6.0
s77
r 7
rge (Ib)
Rema
pieces Ib;
ining Coal Bed Ib]
Kindl ing
pieces Ib
TEMPERATURES
Combustion
Air
Combustion
Chamber
5^7
t^?/ -
^7c)
j"^r
^yy
cf57
firs'
^ L?
.5V/
•C~/ ~7
( ) L? /
£7 / £^
570
Stove
Surface
Wo
V20
Lllo
^2d
/f$0
i/2S
_ y..db< . ,._
V/v
HID
110
JLJ/0
HdO
Opfletty
Catalyst
-^teLer1"^) .pj-e
(^ flltf-f
M. 7S
no
rt.#
11. 0
n tf
J^.So
I H, 2-f
/V.7J>"
y^/y
tf.s
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(
\
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/
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Post
f
\
)
1
1
1
•
NDIR
CO
AS
AY
IS
/.s
/•Y
/^
/,£
;fi
A 2,
/{l
\2^
H~
C02
^o
^5-
^^
fao
s.s
6,0
S.o
ti<0
s^
&*
£o
$°
HC
PPm
^
3dd
3-00
175
/So
l
lib
tw
/oo
70
75
Opacity
Ho/j
2>OCL
3oZ
•2571
2SZ
2 3 %
3S%
J-dZ.
^7*
}#%>
/%"''->
/X'c/l
/z:'^
Comments
( Footnotes)
'7.: 7+ fi'L,-
Comment Number:
-------
Operating Parameters
Run # O Date S^jf-S^V Clock
Time (24 H)
Operator VS - - / /
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
E 1 asped
Time
Minutes
t*&
200
in>S
Zo<£
\
Fuel
Weight
Ibs
6JS
Stj>
^^
/^,Y)
_^
Remaining Coal Bed
pieces Ib;
Kindl ing
(Ib)
pieces Ib
TEMPERATURES
Combustion
Air
Combustion
Chamber
33-?
^/-/^ "
SJS
520
i r
Comment Number:
-------
c_
Stove Name
Run Jf
Phase #
HP
PV
Oregon Method 7 Sampling Data Sheet
Date
[ Train Operators
Clock Time (24 H) /3V.3- I
Sample Box #
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
<
Nozzle Diameter O -
'<2T Cp =- 0
Elasped
Time
0
Meter
Vol
Pitot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac.
O
Box T
Temperatures
Imp.
70
WB
DB
A- "7
Comments
8
,10
/->.
ex
•id)
o
"71
/7
36,
55-
d(
./O
0
'(0
.0(0
,0%
373
.0*
O
73
-74
o
21
o
77
90
3,47
76 o
-------
Oregon Method 7 Sampling Data Sheet
JO
Stove Name
Run ti
Date
Train Operators
Phase
Clock Time (24 H)
f-
Sample Box #
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
Nozzle Diameter
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
.or
Act.
. to
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
WB
DB
Comments
7
3io,S?_
'0
7
OPl
dO
97
-7
ZZ
/97
"
(1-7
sis.q?
97
/Gb
7-s-
7-r
.0X37^
7,5
j^i
2-
ZZ
iK
.C56Z-
ll
231
/of
i
.(6
z
7
7?
/Srj
5
Sletf-
-------
GM'. l
Total
Condensate
<^.^--
FILTER IDENTIFICATIONS
Front Filter-First Filter #•
Front Filter-Second Filter JL
OTHER INFORMATION, COMMENTS
fl
Back Filter-First
Back Filter-Second Filter#
ORSAT DATA
CO,
Analysis 1
Analysis 2
Analysis 3
Average
CO
CO
CO
N
22 2
Atomic Wt. Atomic Wt. Atomic Wt. Atomic Wt.
(32) (28) (28)
Time
Test conditions:
- Tots! AtomJeWt,
-------
Enivironmental Services, Inc.
10260 SW Nimbus Ave., M-8
Portland. Ore 97223
(503i 620-7337
LABORATORY TOTAL -PARTICULATE CALCULATIONS
Source Description,.
Plant __ ..... _ Date ( s ) Analysis
Sampling Date ( s ).^ -^f-g-/ Run # $~ Project #
I. Rinse & brushings of nozzle, probe, and pre-f liter glassware.
Evaporation of. *-$i (ml) o f _ /Qz&s
. 7 3 cV (mg) . Tare.7/.uJr (frg)
- Blank ((.g.g>4.r mg/ml)(. T7 ( ml) = I2.W mg) = SO mg
II. Filter catch(es).
Front filter Final g.tf7/ (mg) - Tare o.*t>7* ^mg) e.2-^
Back-up filter Final ^ r^ r j (mg) - Tare. ^-/r/^» (mg) = 0-ctr?4 mg/ml )( >?-3 ml total
.ml condensed = , ml ). =J,4gg'.h mg
VI. Other particulate catches. =^ _ ' mg
VII. Total ^articulate = I-HI+III+IV-fV+VI
Blanks
Acetone Final _ (mg) - Tare (mg)
mg/ml
Kethylene chloride Final-__^____Jmg) - Tare ( mg )
~ 1
Water Final _ (mg) - Tare (mg)
mg/ml
Other Final^ __ (mg) _- Tare (mg)
~ ' 'ml =_ mg/ml
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
|Time
I3f$
/£
/7
/
0
Y^
52?
'3£
'*?
$Z)
<-fO
3o
i$"
3<>
•30
5o
Jo
3A
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^
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3°
ao
3^
3o
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0
\
1/4
.1/2
3/4
Stove Name
Date S/S'/Z 1
Clock Times (24 H) /ZY2,-
Run # ^"*
Phase # ,^-"
Observer r£'V
Distance to Source "^ 5^^r
Direction to Source /V O
Wind Direction jJoU
Wind Velocity CP — 'Z—
Cloud Cover ;
Plume Background /^t*jt~&
Stability
Relative Humidity
Type Contaminant
Color ^^X^-^^-
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
Run
Bacharach Smoke Spot
Date / / r /V | Operator
Test Time Sample Spot
Number (24 H Elap) Location ' p> Value
ns"
5
1& ^
1ST JL
Test Time Sample Temp. Spo
Number (24 H Elap) Location Valu
Comments:
-------
ORSAT DATA
Stove Name Date
Sample Time
Run # -^ _ Phase # -jL _ Operator
Sample Time 1^ £"^>
,>
C02 02 CO N
Accumulative T.Q.
Net tfZ 12
C02 02 CO
Accumulate b,^ VuT.Q
Net
Sample -Time
C02 02 CO
Accumulate £>, / /^ &
Net
Sample Time
C02 02 CO
Accumulate ^. f j ^ ^
Net £>Z H.7 |.
-------
ORSAT DATA
Stove Name Date 61 £/T~l
Run # ^ Phase # —— Operator "^C''
Sample Time ^
Accumulate
C02 02 CO N
Accumulative
Net
Sample Time -^ )Sl3
A
C02. 02 CO
Accumulate
Net
Sample -Time
C0 0 CO
Sample Time -~H~fc?~
C0 0 CO
Accumulate
Sample Time
Accumulate
Net
C02 02 CO
-------
(3.4Z
Moisture Data
Stove Name Date
Run I _.S Phase # - Operator
27T
Time (24 H) Temperature Moisture
Wet Bulb Dry Bulb Percent
11 cr MY ^u~ __/_!
/4
7
13.6 grr _1
-------
Wood Moisture
_ y _- /•,-* r*~~
Date Y/ 0> / V"/ Test Run # -3
Operator CTSC
FUEL #
1 4M
2 £^
O t^{
A >*— ^ '
6 ^
7. ^4-
8 ^
9 U
10
11
12
Kindling
Meter Me
A
12
^
/,
ll
\(
},
/I
;/
//
B
/6-r
v^S
,a
1-1
a
/5.r
a
^
;f
c
17
14
a
13
IS
,i
I'A
;, .
1$,S
Total Mass 2.4 l-^S
D
j4.^
/^.^
"Ic?
u
IS
^
/6,
'K
/s
E
^^
II
11
D
h
I,
/'• ^
Q.£
n
asuremen
F
;*,r
/31
ar
,^
1^
,4
1^
/^^'
/^
Ll v\ ( f_
Percent Moisture / -f /^
Total Mass (Dry Basis) CO.4lk<
-------
Operating Parameters
.^ ir. > r~f X
Run $ (s? Date o ~~ x9" ~~~ u > Clock
Time (24 H)
*7V/O Operator ^^--•' /''V
Stove Name
Fuel : Initial Cha
Test Charge
Elasped
Time
Minutes
0
/o
A^T
.3.0
3£
^0
^6-
yo
/y^
/JAp
Fuel
Weight
Ibs
373
33.1
32>v
7nj
/ Y Ib
TEMPERATURES ^9^
Combustion
Air
Combustion
Chamber
7^ "
53^"
^3 /
~7 / ,&?
^^S
.f^f
O?'
J"/y
57X
Stove
Surface
2/70
3^2-P
^-//9 ^
//y^
^^
4^.^
/ ^
Afj.^
^/X^
Onaci tv-
Meter-,
^5
X.5"
X/5
y^^r
y^y
x^^
/^/,y
/1,o
Catalyst
,Pre
\
/
i
1
Post
(
\
1
1
•.
\
\
\
. NDIR
CO
^5
A 2,
/-/
1,0
AS
X,L
AS
/X
ho
,tf
C02
/3/?
^
X^f
75
^~r
3".i
f^
,f-^
/?^
6*0
HC
ppm
2(^>
225
$M
30 ^
Mo
37d
370
2(co
3/5
rfO
Opacity
3*Z
J&
<^/jj
t??:
3^
, '-^ / '—^
±?c^^
_i
*y -""i i, "/
(j^ X • x -'
Comments
( Footnotes)
^^"^rT'vv ^
Qfpt'lH- / &9 '*$*'' " -/^'
^v/^ /2 ^ ^
Q.i.bS£ £) T& ^/2 '"' f>
•"^O-i -^ /"^^ <^>' ^ ^"
^"^^; je/^ ^
'**" * ^-
^-'^""/M^^
Comment Number:
-------
Oregon Method 7 Sampling Data Sheet
Stove Name _
Run i? ^
Sample Box I
Probe
Probe Material
-------
pav,.. 2
Oregon Method 7 Sampling Data Sheet
Stove Name H@ Date o | b lo \
Run H
Train Operators
... - ..- .. M ^
6^/fkAn^ Phase i Clock Time (24 H)
"^ /
Sample Box # Stack Dimensions
Probe. Len
Probe Mat
Elasped
Time
10
H-2-
HI\
Mk
•
gth Barometric Pressure
erial
Nozzle Diameter
Meter
Vol
m»
^«^o
3^,1)5
pi fnt
AP
,003^
rOtS§
'W3
Orifice AH
Calc.
/3/7
r^7
•77
Act.
.z°T
*',<
t^
Stark
Ts
^73
2>7?.
392,
Gas Meter
T in
£*
31
T out
§7
8^
Vac.
^3
555-
33-^
Rnx T
Bf.C
Bo.
Temperatures
Imp.
&£
UB
DB
((li^MS.. comments
^^ S Ml
-*n 74
o?«T
-237
-------
Environmental Services
13SO NW Lancashire C1
Eeaverton. OR 97006
Test (
SOURCE SAMPLING-LABORATORY ANALYSIS OF PARTICULATE SAMPLE
Project # /P&S/5
w.
Date of Test
CONDENSED WATER DETERMINATION
Impinger:
Final weight
Initial weight
Net weight
fl
/T^T (a
S33. /
32
S&Q of
J53Z*/
32, r ' 3 ./
f3
^J2Jr. 7
*£18',3~
o .0
5^4
•7/7.S-
~7/^S
r-4
Total
Condensate
4/.2.-
FILTEr. IDENTIFICATIONS
Front Filter-First Filter #&' /•
Front Filter-Second Filter J£
OTHER INFORMATION, COMMENTS
Back Filter-First Filter
Back Filter-Second Filter#
,;»/*/
£-'
CRSAT DATA
Analysis 1
Analysis 2
Analysis 3
Average
CO,
CO
CO
CO
N
2 2 '2
Atomic Wt. Atomic Wt. Atomic Wt. Atotn5.c
<44) (32) (28) (28)
Time
Test conditions:
-------
Enivironmental Services, Inc.
10260 SW Nimbus Ave.. M-8
Portland. Ore. 97223
(503. 520-7337
LABORATORY TOTAL -PARTICIPATE CALCULATIONS
Source Description.
riant ______ . ___ Date(s) Analysis, ? ~ '-• -'<~tC> _
Sampling Date(s;; £^&-f/ Run # 7 Project #
I. Rinse & brushings of nozzle, probe, and pre-filter glassware
Evaporation of.. ^-^ (ml) of
Final 72. S-gn" (mg) - Tare <.7*.&i63 fog) - /
- Blank: ( (. c?.^4-T mg/ml) (. "Sfcfe- ml ) = n.1/? mg } =
II. Filter catch(es). F^-IZ— 3#_££Z_
Front filter Final. ^-wg (mg) - Tare 0 •&¥<>_ (mg) 0-v
•*• Back-up filter Final,c>.^77j_(mg) - Tare^./ra./^ t(mg) =_c'-
.
III. Hydrocarbon obtained by solvent extraction of water in
in impingers and .bubblers,- _ n
Solvent used & itZ &JL ^ ?? ** _
Final 7/. »f ^ L ( mg ) - Tare 7/, 3l^^~ (tog ) it^V /^-/. 7 ^
- Blank! (.g?.t.>-^(3mg/n>lj(' T-T .ml) =.),?/ mg ) =, f4^.? _mg
IV. Particulate from evaporation of water in impinger and
bubblers following extraction.
Final 70, ?p73jmg; - Tare\7°- ?°K> (frg) '^>e^r 2. cr. 5
- Blank ((^P-wtf mg/ml)( 2.30 ml total
ml condensed =_ /3^T ml) =
Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware.
Solvent used 'Ae,<3Zn-*. • ^°~7
Acetone Final
=
Methylene chlorii
=
Water Final
=
Other Final
r=
(mg)
rmg/
de Final
me/
.(mg) -
mg/
• (mg) -
m&/
- Tare
mi =
(mg)
ml =
Tare
ml =
Tare
nu =
(mg)
"mg/ml
- Tare (
mg/ml
Jmg)
mg/ml
(mg)
mg/ml
_ _
Final .72,/£ ^
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Time | 0
1/2
3A
Stove Name
Date
Clock Times (24 H)
Run # _
Phase 1
Observer
Distance to Source
Direction to Source _
Wind Direction /^—'
Wind Velocity
Cloud Cover O
Plume Background
Stability
Relative Humidity
Type Contaminant
Color
No. of Readings
% Opacity
0
10
20
30
40
50
60
60+
Units No.
Minuses of Observation
-------
Bacharach Smoke Spot
Run
Date
Operator
Test Time Sample
Number (24 H Elap) Location
_
p'
Spot
Value
Test Time Sample Temp. -
Number (24 H Elap) Location Va
7
4JL
4± ii/T
AT [5)7
_C2_
0
o
3
Comments:
-------
ORSAT DATA
Stove Name ; Date _
/** —•'
Run # fc.' Phase # Operator \C.
Sample Time Ofi -2.3
Sample Time
C02 02 CO
Accumulative
Net 7-0
S T
co2
02 CO N2
Accumulate . v, ,''X ifyb -^•T
Net Si /4.4- O- Y
Sample -Time
co2
02 CO N2
Accumulate
Net
Sample Time
co2
02 CO N2
Accumulate
Net
Sample Time
co2
02 CO N2
Accumulate
Net
-------
Opacity Transm.jssome;feer--Meas'urement
Run
Date
''_ ' i'- •' :" ' Operator
Pretest— C-a-Kb rat-ion- OK
Opacity
L
21
2 1
/W \cr -bUl \cd& 24
Post Tes-tCali brat-ion OK
Flue^Gas
"
'V 1:
* Record every 15 minutes
** Record every 5 minutes
D
/
Tfrfe"
7£
* r ^~*f""
*»»
_£L
7?
-------
Moisture Data
Stove Name ; Date
Run # •_- Phase # Operator
/re?
Time (24 H) Temperature Moisture
Wet Bulb Dry Bulb Percent
!3>T ^o 14
-------
Run 9
Date
Operating Parameters
Clock Time (24 H) / //V /
Stove Name
Fuel: Initial Charge (Ib) 2. %\
Test Charge *$? _. pieces
Remaining Coal Bed (Ib)
payc
Operator
i
JP
. 3> Ib; Kind! ing
pieces
Ib
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Stove
Surface
wrc4*y
Combustion
Air
0
- V
2 c?(
Combustion
Chamber
NDIR
^25
-X%&
7
3^5
o
^&
£L
3S7*
S3Z
Comments
( Footnotes)
f ~i
I /• /
~ \
JL^L
f,D
1SL.
1,1
3.00
737
6/0
U
/J.O
Mo
20 n
75
*^S- r
^41
Comment Number:
-------
Operating Parameters
Run H / Date &-(£'& /
•
Clock
Time (24 H)
- ' - 7
Operator ^A^ / /
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
Elasped
Time
Minutes
(dO
^V
f > ^x™""'^
s v»-«^
<^~
$.v
7 7
7.1
(<,1
pieces
Remaining Coal
Ib;
Kindl ing
Bed Ib)
pieces Ib
TEMPERATURES f^
Combustion
Air
Combustion
Chamber
^77
673 -
&I3
&J D
(057
(#(si
& & /
fa^^
6/5
fW
5to6
(tV*
fa.
>
>
Stove
Surface
sw
T80
^}OL/
S (0O
fbo
,<7S
*75
£5O
£50
S3£
500
ty%£>
H%®
Meter
y^5-
/^.^
/5.^
/ **7 ^^
/ f?C / sx
/ J>; ^
y-7.^
J2S
J*> o
I5.S
/y.o
/ H,5
I 3.S
i3,5
Cataly
•'/
(
1
i
'-
P<
t
ist
\
\
1
/
t
\
/
l
1
NDIR
CO
/-/
/.y
l.o
/,/
iM
/,/
f<0
l,i
l
I.I
l,l>
C02
7S
7.5
7,n
to
75
j>,i
^.0
^,f
7/3
f ^
&o
7,c?
HC
ppm
M»
27D
32o
310
^0
MO
ZZo
&v
MO
ZSS
3&
3-50
21*)
Opacity
3D?~
HcJo
<^/.
3.6 7-o
30^
J^ if ' £r
^*) • C'?
y^7u
v <%
.?^7y
35%
Lid7o
Comments
( Footnotes)
'/^07/j£r/
V ^
.^fi'i-x KJ% /<5, (J ^
,., ,>/1 fn f £ /'. /
-------
Run 0
Date
Stove Name
Operating Parameters
Clock Time (24 H)
Operator
Cc "
-~ V-' / /
Fuel: Initial Charge (lb)
Test Charge pieces
Remaining Coal Bed (lb)
lb; Kindling pieces
lb
Comment Number:
-------
Run
7
Date
Operating Parameters
Clock Time (24 H)
Operator
Stove Name
Fuel: Initial Charge (Ib)
Test Charge pieces
Remaining Coal Bed (Ib)
Ib; Kindling pieces
Ib
Elasped
Time
Minutes
I If
SL0D
Fuel
Weight
Ibs
3 3
c?7
•
TEMPERATURES ^^
Combustion
Air
Combustion
Chamber
£72
.^83 -
1 } r :'
Stove
Surface
^20
H20
'Vto
-Opttctty-
Meter
W.75
tf%
2^/r
Catalyst
-,Pre
\
1
1
Post
^
1
j
NDIR
CO
1,0
1 ^
2.0
C02
5,0
K
-------
Stove Name _
Run t 7
Sample Box tf
Probe Length
Probe Material
Phase i
2. Stack Dimensions
. Oregon Method 7 Sampling Data Sheet
"0 . Date S/6/&/ Train Operators
Clock Time (24 H)
......~ y^ —
3^ Barometric Pressure £L 9. B/
Nozzle Diameter O, S7?Z40T
__ _£S
Jt
OT
-------
pac,-
2,
Stove Name
Run #
Oregon Method 7 Sampling Data Sheet
Date 8/6/Af
Phase
Clock Time (24 H)
Train Operators
Sample Box ff
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
Nozzle Diameter
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
WB
DB
Comments
US'
^33
'67
9
(0*
£79
76
373^
o
7?
16V
((0
o
n
n
U
0
,f7
7?
-------
Oregon Method 7 Sample Recovery Data Sheet
1
£
Stove Name
Run j?
Box ;?
Date
Phase #
Clock Times (24 H)
CONDENSED WATER DETERMINATION
Impinger: #1
Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
)Front Filter-First Filter #
)Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash _f/ ' "^>
Blank
.763,
Back Filter-First Filter I
Back Filter-Second Filter #
CREOSOTE COUPONS
Plate Location
Plate Location
Total
Condensate
—*•—
Plate Identification
Plate Identification
Tape
Date
Mg
Date
Mg
Final
Net
-------
:»«•'..!": Enivironmental Services, Inc.
10260 SW Nimbus Ave., M-8
Portland. Ore 97223
(503) 620-7337
LABORATORY TOTAL-PARTICULATE CALCULATIONS
nli pnt .//-^ -f WC £• >• l(S Source Description,
Plant ___ .. ____ Date(s) Analysis,.
___ .. ____ ,. •
Sampling Date(s).£-£-fr7_ Hun # >" Project #
I. Rinse & brushings of nozzle, probe, and pre-filter glassware
Evaporation of. z 3^ (ml) of_ Xg/-Vz7>xg> ,
Final 7z*f9fi (mg) - Tare ^ . 6 r? ?( mg )• .^V- ajy, j
- Blank i (. p.c-^r mg/ml ) ( . lie* ml ) = /£?.T>r mg) = 2
Filter catch(es).
-i CF^ont. fjJJ^rL^ Final.g. yw ( mg ) - Tare.^- ^»7.(mg)
-)b" + Back-up f ilter\£jAalT^?^*(-B)g ) - Tare. g.ig) x^/ 3 ^ - 6
- Blank ( ( gj.c?cr7^ mg/ml )(_. ^ja.'Hanl total
ml condensed -^Ik.-k ml) = /.3 ,3>4/./ mg
— ^"^ —
.
Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware. ^
Solvent used /4g<3fr£rXx ^ ?^£ ^
Final ^. 3 g^^- (mg) - Tare /7.9/?2. (mg) ->*e^r jfj.o
- Blank (~(_&>o4$ mg/ml)(_ 3>4£ ml) = >f- r? mg) =,3>4'>,4 mg
VI. Other particulate catches.
VII. Total particulate = I+II-HII+IV+V+VI
Blanks
Acetone Final (mg) - Tare
= ^ mg/ ml -
Methylene chloride Final (mg)
mg/ ml =
Water Final (mg) - Tare
= mg/ ml =
Other Final (mg) - Tare
— mg/ mj. —
(mg)
mg/ml
- Tare
mg/ml
Jmg)
mg/ml
(mg)
mg/ml
(mg)
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
fTime 0
'2.3?
W
36
37
ffit
3(*
37
$7
tt3o
M
%l
35
>y
7'
?c
<)^~
*?c
i
1J?
1/4 1/2
20
V*r<2
^
2-**
3o
%o
^
tt
^
^
3C?
20
7,o
2.^
3O
^
XS"
3r
N f^\
/ ^
ao
Vb
^<
^,j
^0
/5-
X^T
?P
^o
3/4
/r
^c?
2f
30
y^
• —
^
s ^
r
<+-o
'~rC?
2.0
/S
} f^^\
~l°
IP
Time 0 1/4 .1/2
{L**£L
^T
— Aut
Pu-c -
A.V. -
^d
\
'27
36
/ ^/
vi££
^
i "7
3/4
ifc?
Stove Name
Date £/£
Clock Times (24 H) //S~7
Run # "7
Phase # ^£*7~'*~z&~f~
Observer /fe-~T"
Distance to Source "^ S^/rT"
Direction to Source /^G*
Wind Direction /^— ^
Wind Velocity /•*_--'£'-£.
Cloud Cover £?
Plume Background "t^f-f^x-
Stability /{r^-^>
Relative Humidity
Type Contaminant
Color /C*~yh£cjL
No. of Readings % Opacity
0
10
20
30
40
50
60
60+
Units No.
Minutes of Observation
-------
ORSAT DATA
Stove Name
Run #
Phase #
Sample Time
C0
CO
Accumulative i,y ^ r
Net •) L r
Accumulate
Net
Sample Time
Accumulate
Net
?-c
Sample Time
Accumulate
Net
Sample -Time __]_
C0
CO
C0
CO
Accumulate A ^-
Net • Ti5
Sample Time _
r/4
C0
CO
C0
CO
, 7
Date
Operator
-------
be
^ A
r/
T 6
9L
»0 uoi^-Bjqi.-!
uny
-------
Moisture Data
Stove Name
Run #
Phase #
Date
Operator
Time (24 H)
Temperature
Wet Bulb Dry Bulb
Moisture
Percent
14
3
-------
Run
Date
Operating Parameters
Clock Time (24 H)
P-y
Operator
Stove Name
Fuel: Initial Charge (Ib) Remaining Coal Bed (Ib)
Test Charge 8^ pieces 3>L*f Ib; Kindling S^(^L pieces ;?. «/ Ib -/
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Met
Catalyst
•,Pre
Post
NOIR
CO
C02
HC
ppm
Opacity
Comments
( Footnotes)
32.1
30,6
AS"
35
V-2/
/Jo
lo
7/9
IW
J-So
Ai,
its
^iA
,/7.f./f;
3-
ZdL
CommeiU Number:
^/^
,55
z^z.
A)1// 5'
-------
Run #
*$$
Date
Operating Parameters
Clock Time (24 H)
Operator
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
pieces
Remaining Coal Bed (Ib)
Ib; Kindling
pieces
Ib
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
flpacity
Meter.,
Catalyst
.Pre
Po^t
NDIR
CO
C02
HC
ppm
Opaci ty
Comments
( Footnotes)
fi. f.
7
2oo
lt.1
tf.S
50
/So.
no
.0
337
2.0
//o
2$
/ £ /»
rUL
/&/
-------
Operating Parameters
Run H 5 Date tf " 7" ^ / Cl'nrk
Time (24 H)
Stove Name
Fuel : Initial Charge (Ib)
Oper
a tor \ ^> )"'?
Remaining Coal Bed (Ib)
Test Charge pieces Ib;
Elasped
Time
Mi nutes
1VX
/^p
/SS'
Fuel
Weight
Ibs
A?,£?
/Z 1
II. b
Combustion
Air
Kindl ing
TEMPERATURES ^^
Combustion
Chamber
i
v/s -
HI2-
.u r r
Stove
Surface
3/0
•300
2%V
'6' -/ J
•eptKH-t^
Meter^
/7,r
J7.V
^7S
4 -> V
Catalyst
,Pr|e
••
Po^t
i
t
i
i
i
I
\
pieces Ib
NDIR
CO
,/<>-
7T>
-jr
X'O
C02
?-o
^ 9
,^v?
HC
ppm
/?o
,„-,
•^
Opaci ty
s/7
V "'
/ ' '
-
Comments
( Footnotes)
/i7
/^" I/-., . (1 IV
Comment Number:
-------
pa I
Stove Name
Run #
Oregon Method 7 Sampling Data Sheet
/, £"*/ Date ? -7-8V Train Operators £><-
Phase I
Clock Time (24 H) 0905"- 1/(4Qfv
C (<. <". OZ
Sample Box #
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure 49-77
Nozzle Diameter
33
•sr
o
0
76
D
o
73
30
-------
Stove Name
Run I
Phase *
Oregon Method 7 Sampling Data Sheet
H@ Date %"-? -8 / Train Operators
Clock Time (24 H)
Sample Box it
Probe Length
Probe Material
Stack Dimensions
Barometric Pressure
Nozzle Diameter
Comments
m
&8
-------
Stove Name
Run £ ^
Box # /
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase #
Clock Times (24 H)
CONDENSED WATER DETERMINATION
Impinger: #1
\Final Weight £o/-Y
tial Weight
Weight
FILTER IDENTIFICATIONS
Front Filter-First Filter #
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/ Front Filter Wash
Impinger Wash
Blank
CREOSOTE COUPONS
Plate Location
#3
#4
57. 3
,0 7&.Z
Back Filter-First Filter #
Back Filter-Second Filter #
Plate Identification
Tape
Date
Mg
Plate Location
Total
Condensate
l a te Identification
Date
Mg
Final
Net
-------
Laboratory Total Particulate Calculations
Stove Name . _ _ Date of Sampl ing
Run # ^ Phase # _ Date of Analysis
Box # / _ Analyst
I. Rinse & brushings of nozzle, probe, and pre-filter glassware.
Evaporation o£_ \'l L- (ml)
,
' ''
Final'so. ?t?/ (mg) - Tare\ 70.^f.rfag)
- Blank ('(.g^f mg/ml) (. _ r?2- _ml) = 7 ?T*- __ mg) = _f.^»^6 , mg
J- x-
, V-^ Xfi; Filter catch(es).
Front_filter ginalQ.s-s^.Cmg) - Tare
__ .
+ Back-up filtertyinalg.yy / <7
- 3ianlc( (_^-g^i^ mg/min. YC ml) = . /. T/ mg) =
IV. Particulate from evaporation of water in impinger and
bubblers following extraction.
Final. 7/. osOung; - Tare 7
- Blank (' ( g«c^7^ mg/ml ) (^ 2. ^j ml total
ml condensed -_ 22ttf> ml) s /.
~ '
.
V. Particulate from solvent rinse of impinger, bubblers,
and post-filter glassware.
Solvent used
Final TJ-.Wrf (mg) - Tare,-7y. o^v-^ (ing)
- 3lank ((.^.g^ mg/ml )( J>S"3 ml) = / r. VZ mg ) =
Acetone Final (mg) - Tare (mg)
= .rag/ nil = mg/ml
Methylene chloride Final _(tng) - Tare (mg)
= mg/ _' ^ml = ^_ mg/ml
Water Final (mg) - Tare (mg)
= mg/ ml = mg/ml
Other Final_ (mg) - Tare
= mg/ ml = mgyml
VI. Other parxiculate catches. -t mg
VII. lotal particulate = I+II-HII+IV+V+VI =JU±^.
Blanks
-------
Bacharach Smoke Spot
Run
Date
// / .
Operator
Test Time Sample Spot
Number (24 H Elap) Location H> Value
-11
1C IA
LL2J
'37
o
_^
Test Time Sample Temp. Spc
Number (24 H Elap) Location Vali
U
£4
^_ 2Z£>
C *1.&0 ^
Comments:
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
iTime
1/2 |3A
->i )
//CO
oZ.
/r
^ J
p.®
/r
*
Time | 0 |
.1/2
AS"
ro
lo
v
3A
Stove Name
Date
Clock Times (24 H)
/ )
Run # _ \: t-c^i ^ ,;
Phase #
Observer
.-7C
A — '
r'CT
Distance to Source
Direction to Source
Wind Direction
Wind Velocity
Cloud Cover
O ~ f
Plume Background
Stability
Relative Humidity
Type Contaminant
Color /
No. of Readings
% Opacity
0
10
20
30
40
_5rL
60
60+
Units No.
Minutes of Observation
-------
ORSAT DATA
Stove Name
Run #
Phase j?
Sample Time
Accumulative
Net
C0
co
Sample Time /£;> /
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
co2 o2
CO N,
0.4- 4£i
\
co2 o2
3.4- /'^-
2,4 ,/ 7. 2
C0
CO
CO
CO N,
Date
Operator
K
/- \
L:
/ C - ^ x,
a .
4 C
-------
Moisture Data
Stove Name Date
Run # •'' Phase # Operator
1 02
I IT
II 14 Wo 3. ^/
Time (24 H) Temperature Moisture
Wet Bulb Dry Bulb Percent
-------
Run
Date
Operating Parameters
Clock Time (24 H)
Operator
JS'.-7
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
Remaining Coal Bed (Ib) ^
Ib; Kindling (SgcX/vv/-^ pieces 3-1 Ib
Elasped
Time
Minutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Meter
Catalyst
Pre Post
NDIR
CO
C02
HC
ppm
Opaci ty
Comments
( Footnotes)
0
/{I
/
315
2.5,0
.2UL
/2S/
tl
3
ISO
22.
so
-/
J-I..T
ii
1.0
•2S
IZjS.
10.
.0
5O
Jti
/XD
£c
is, so
,(00
5*0
Comment Number:
-------
Operating Parameters
J
Run # tf Date SVy/£ / Clock
Time (24 H)
Operator ^.^-^ / /
/ J I
Stove Name
Fuel : Initial Charge (Ib)
Test Charge
Elasped
Time
Minutes
(£O
70
A5-
"SD
fr«r
io
75
10-0
/d-f
I/O
//<
/^/o
yjff
Fuel
Weight
Ibs
MX
/ 0 £
1 o*\ ^
\L$
//, 2-
/^
y^y
/0,<3
7. £
?„?
f <5
^•(^
S1,^
ff.l
Remaining Coal
pieces Ib;
Kindling
Bed (Ib)
pieces Ib
TEMPERATURES ^2.
Combustion
Air
Combustion
Chamber
SW
f\ ^\ / ""
^ j <—^ ^*
J~«T7
S*l&
>r/y/]
V ^c^
^7
W3
5^^ <^
3^6) £J
H,l^
W?
YJ6
Stove
Surface
ISO
Wo
^30
^30
VJo
W£
^D
*v
-Vf 7
J5~0
3^0
Mo
Onari tv^
Meter
<^
/* -
)S,f
/ &i O
/ (g , CJ
l bo
f
/7,£>
n,o
/X.o
nrf
n<^
Catalyst
Pre
\
PC
r
NDIR
CO
,k>
fc
ft
.55
,H5
fa
•If
o
}.o
2£
W)
HC
ppm
t*>
HO
1)0
W7
/.<*'$
fdO
pff
10
{#»
i/n
Opaci ty
,•0?
*~J /&
£?-<*?
£~ 07
Comments
( Footnotes)
^TCI^^
Mi'/
-------
Operating Parameters
Run # ^ Date ^^2^/ Clock
Time (24 H)
Stove Name
Fuel : Initial Charge (Ib)
Rem
Test Charge pieces lh-
Elasped
Time
Mi-nutes
I$D
l$£
jVD
•/fe'
'SO
16^
l(eo
/&<
170
1 7J>
itfD
IKS'
\W9
Fuel
Weight
Ibs
7,f .
?.r
6X
i,y
^/
vy » O
(,_) t v y
^ ^
/y
/ / b?
Y.J
'/.i
3- ^
3-6
aining Coal Bed (
Kindl ing
TEMPERATURES ^
Combustion
Air
- - -
Combustion
Chamber
y/^
?fZ- -
/ s\ ^*i ^t
fvjS
k#*f
S<*7
5"^Z.
^?/y
SSt?
s-$y
^0
V77
^^7
Stove
Surface
3//9
J^JO
J§-^
*iOD
L/fiO
you
2$o
3JO
HbO
Mf)
3?O
3^0
$70
<&t dr" i-vo- •
* j
"Meter
I y r\
I. 0
77 Q
n,$
\7 £
J7.o
)7 £
/7/f
1-7.0
17,5
n. 76"
Ib)
Catalyst
.Pre
I '
1
t
1
1
i
Post
/
\
i
'
i
t
\
_ .
Oper
•a tor
Pieces Ib
NDIR
CO
3^-
>(f
* ^-^^7
^//j
,w
^
r^7
r^7
^
l?^
^
^
C02
^,^
?^)
?,-)
3<9
?,0
?^
3,5
? .
7 ^
2 -5
1 <
*.
5T>
A/<
W
Opacity
57^
3"^-
^T/2
£?o
S?
5%
r7
^%
37
5%*
0%
J7,
0"%
Comments
( Footnotes)
/ _
/ x?
^/U-v^C^ (/>Jt>7Z'> (W>
C-- A V^^^.
^tvs
c^
Comment Number:
-------
Stove Name
Run #
9
Oregon Method 7 Sampling Data Sheet
••&&.
Date
Phase i!f
Sample Box I fr&fif tf Z-
Probe Length _3>
Probe Material
Clock Time (24 H) /3/fr-
Stack Dimensions
-------
Oregon Method 7 Sample Recovery Data Sheet
,
f
Stove Name
Run #
Box # - _
Date
Phase #
Clock Times (24 H)
CONDENSED WATER DETERMINATION
#1
v^.
Impinger:
J
Final Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
Front Filter- First Filter #
Front Filter-Second Filter I
WASH IDENTIFICATION
Probe/ Front Filter Wash
Impinger Wash
Blank
#2
#3
Total
Condensate
'•3 17/.V
,
0
Back Filter-First Filter #
Back Filter-Second Filter #
CREOSOTE COUPONS
Plate Location
Plate Identification
Plate Location
Plate Identification
Tape
Date
Mg
Date
Mg
Final
Net
-------
La bo rato ry Total Particulate Calculations
11 * '"
Stove Name . Date of Sampl ing
Run 2 tf Phase # Date of Analysis
Box # ^ Analyst
I. Rinse & brushings of nozzle, probe, and pre-filter glassware.
Evaporation of. - 7-' (ml ) of
Final ?•*•&? 7 (mg) - Tare_^.__V£rJ mg )
- Blank ((.,.-- ,-.4,r ,mg/ml )(. /?4 __ml ) = ?-'?o> mg ) = .-I -'• ^ mg
J? (fT} Filter catch(es). F£
o- (mg) - Tare '••*''/& (mg)
^ __ —™-^^^^^— _.._ __ —
+ Back-up filtefy^inaly'.rg^^ (mg) - Tare. <7.«^7 <,-o (mg) = _
^,-:, . . .
III. Hydrocarbon obtained by solvent extraction of ' water in r. w9. 3
in impingers and bubblers . ,7
Solvent used ~r - , -
Final 7f.$-^>Mmg) - Tare 70. 53^9 (mg) .^<^r t ??•. ° ' s~
- Blank (( ^ 3«/*< ,
Final 7*.7f*9 (rngj- Tare,^. 27?Xmg) ^-^ ^r. /
- Blank ( ( . c?>o4rmg/inl) ( j<4 ml) = )4-l3 mg) =. ^/.Q mg
Other particulate catches. = m
VII. lotal particulate = I+II+III+IV-tV+VI =_/_r_/4Ljng
Blanks
Acetone Final (mg) - Tare (rag)
= mg/ ml = mg/ml
Methylene chloride Final (mg) - Tare (mg)
= mg/ _ml = _ mg/ml
Water Final (mg) - Tare (mg)
= >.m£/ .m^- ~ mg/ml
Other Final_ [mg) - Tare (mg)
ml = mg/ml
-------
Bacharach Smoke Spot
Run
Date
Operator
Test Time . Sample
Number (24 H Elap) Location
Temp.
Spot
Value
Test Time Sample Temp. S
Number (24 H Elap) Location Va
c
JL^7
no
JL
V
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
Time |0 HA | 1/2 13/4
' 5?
10
57
10
1°
to
fC
/2
/r
/r
5
Time I 0
1/2 I 3A
/o
r
(0
,r
r
5"
Stove Name
Date
Clock Times (24 H)
Run # 9
Phase #
Observer
Distance to Source
Direction to Source
Wind Direction xl
Wind Velocity
Cloud Cover
Plume Background
Stability
Relative Humidity
Type Contaminant
Color
No. of Readings
Units No.
/
% Opacity
0
10
20
30
40
50
60
60+
Minutes of Observation
-------
ORSAT DATA
Stove Name
Run ;?
Date
Phase #
Sample Time _
Accumulative
Net
Sample Time _
Accumulate
Net
Sample Time _
Accumulate
Net
Sample Time _
Accumulate
Net
Sample Time I
co
co
Accumulate
Net
C0
CO
"* fl - " } "
— - ^ i ' •*'"
) 4-
C0
CO
& 7
C\ , 7
C0
CO
is 7 -
CO
Operator
-------
ORSAT DATA
%
Stove Name Date
Run 5? , Phase # Operator ^
Sample Time , '• " -. -
C02 02 CO N
Accumulative 7
Net
Sample -Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time //-'/ ?
f
C00 00 CO
Accumulate "?.(^.
Net J.O
C02 02 CO
C02 02 CO
C02 02 CO
-------
Moisture Data
Stove Name Date
Run # ,, Phase # Operator
4-
Time (24 H) Temperature Moisture
Wet Bulb Dry Bulb Percent
. ^ s- - J^*a
//c? 3/i& -<- ^
-------
Run ti
Date
Operating Parameters
Clock Time (24 H) /OlS&
pa
Operator
\'S
Stove Name '_
Fuel: Initial Charge (Ib)
• Test Charge pieces J2 $
Remaining Coal Bed (Ib) £2.
Ib; Kindling v^Vu^vu.^ pieces
a.
- "7
lasped
Time
inutes
Fuel
Weight
Ibs
TEMPERATURES
Combustion
Air
Combustion
Chamber
Stove
Surface
Meter
( Catalyst^)
TPYe Post
NDIR
CO
C02
HC
ppm
Opacity
.
Comments '
( Footnotes)
£Z
J//
17
Wo
SO
Q
0
51D
f-o 'z-
20
&LL-31
fill 2,
A52.
/7s
4
7$
2ii
63?
2,0
0
SO
9/,7
Comment Number:
£50
311
-------
Run *
Date
Stove Name
Operating Parameters
Clock Time (24 H)
Operator
Fuel: Initial Charge ("
Test Charge
pieces
Remaining Coal Bed (Ib)
lb; Kindling pieces Ib
Comment Number-
-------
'-1 Run 1 /£)_
„ Stove Name
Date
Operating Parameters
Clock Time (24 H)
Operator
, Fuel: Initial Charge (lb) . Remaining Coal Bed (lb)
Test Charge pieces ,,. ^^ ~—~
Comment Number:
-------
Operating Parameters
Run # /O Date ^^ ^L
3,7
rge (Ib)
Remaining Coal
pieces Ib;
Kindl ing
Bed (Ib)
pieces Ib
TEMPERATURES £>^
Combustion
Air
Combustion
Chamber
7£>CX
/ ' tmJ 1 .A
\/y / ^^
fas?
t^x /^ /
XH?
5^7
SO?
SOD
Wtf
^J5
^v ^
^2
^70
Stove
Surface
X1Q
3X0
370
^7/0
2>$0
IV 3
320
MO
3oo
3Dv
2^0
$5-0
Opoc. i ty
Meter
/&..*
I7.o
j ,7ff
n.s
i&O
/8,t>
fffrf
]%£
JX.D
i%.o
t% <
IVO
Catalyst
.Pre
5?3
ttf
ffft
Y
!
1
Post
6/3
5^2.
6ft
^oy
f-" •JCV'
•J •J 0
Jte
S5&
5/M
,5*/0
\M
V^>
3?t
NOIR
CO
yo
HI
36
,HD
,y3
#*>
,10
'.io
*3fe
,30
,/f
M
C02
^
V*
3.0
lo
3,0
2,7
^
3.6
^\ o
^\ '**
*i*o
3>
HC
ppm
10$
to
iio
/oo
U
Vs
<%o
fro
75
7,<
70
110
Opaci ty
'As,-)f£^ $ /W
^"%^&/%s£
$£?/* */' '*- ££ **& 1 '/i.
rf/I S^'fio
t^ /ty /^T^i ft*
r
Comment Number: / «5 /
Ju)
-------
pa,^
Operating Parameters
Run it /LS Date &/2fZ~/K' / rinrt
Time (24
H)
Stove Name
Fuel: Initial Charge (Ib)
Oper
a tor .^^5' X"/*
/
Remaining Coal Bed (Ib)
Test Charge pieces Ib-
Elasped
Time
Minutes
3&
2SrO
2&6"
tfo
3?<<
So*
Zo$
Fuel
Weight
Ibs
3.7
3.y
3./
3, o
JY
2,7
o2,6
Combustion
Air
Vf.-Lr '^
i
1
Kindl ing
TEMPERATURES O2
Combustion
Chamber
J6.7
S7I "
S<*7
_SS£
1?o
^KD
-
"i :-'6
^•/4>
-/_
Stove
Surface
P» cxr)
<> n Ls
270
3W
325"
JTO
3££
35"^
2<$^5
. ,
44
fin «r i 1 ii
•ypciL I ty
Meter
I7J
/Ko
nf
/ *^' —
/ 7, 73"
/7^
/^s.vx
•'.v.:. -.
Catalyst
•,Pre
43?
'¥•
— -
Post
ft57
?s>
^m
T?V
v-ir/
• '• 1 0 -i
"X ^
--^ <5
••
pieces Ib
NDIR
CO
M
f &L \ t j
,7«•
i^r
./^.
Opacity
JO
Zc
^0
7 f
Comments
( Footnotes)
J^T %±ZJ?T^
ft ^
p/'^^^i:^^ ~f~tJ ) Yg
(cjj / v -y (?
r ^ ,V? /? ,
jtzr/V^ c'- / * <- »- " IA
Comment Number: ^
-------
Stove Name
Run t '
H@
Oregon Method 7 Sampling Data Sheet
/.
Date
pat,.
Train Operators
phase f
Clock Time (24 H) /O
Sample Box (H
Probe Length
Probe Material•£< •£
Stack Dimensions
(o '
Barometric Pressure
Nozzle Diameter
" 1
- 0.8-0"^
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac
Box T
Temperatures
Imp.
WB
DB
o
Comments
8
O
S-l
O
67(0
V6
O
6?
1
, 00
•57
12.
0
S3
O
&L.
£0
.0)5
3>3
3\H
(3
6 01
,33
cr>T 1ST
3o
#7
Ar
87
s-v
/o
S'O
/7
6s-
-------
Oregon Method 7 Sampling Data Sheet
Stove Name HO n,+« 2-^7n<:1nnC
Probe Length Barometrir
Probe Material
Elasped
Time
^ 40
£9
•
Meter
Vol
SB1.7C
""• ' 1 1 »-
- -_
••— ...- .. ...
•
Pi tot
AP
— -II „
*y& /6
I"-
- • •• „
-* — -
— i
Pressure
(24 H)
Jt . c,
Train Operator
4o o£oe
*s
i-^~ 7 Acu.00^
— — i i •
Nozzle Diameter
Orifice AH
Calc.
&
I... — _
•- •
•""• • i—
Act.
-7,0
ISC-
• -
Stack
Ts
J.07
5^3
/^
—
Gas Meter
T in
?*•
.— .HIM -II- ., ,..
* AM*A cAo^
•—•••'• i . _. . „
— — —
Temperatures
Imp.
^
i .>.
HB
i
DB
/
Comments
C3"8 6> C^> e^-r ^o
~" — . _
_
> <7 5)
-------
Oregon Method 7 Sampling Data Sheet
Stove Name
Run I *
HG>
U'S'A
Date
I
Sample Box #
Probe Length
Probe
Phase # <~_
2. Stack Dimensions
Clock Time (24 H)
Barometric Pressure
Nozzle Diameter
Q
Elasped
Time
Meter
Vol
Pi tot
AP
Orifice AH
Calc.
Act.
Stack
Ts
Gas Meter
T in
T out
Vac.
Box T
Temperatures
Imp.
MB
DB
Comments
IT
O
60 &
So
. 75
• 10
1 10
O
^67
/oo
0
637
//.o
III
O
o
O
00$
O
0
c
^87
73
O
6JU.
93
O
76
O
0
S li
o
570
*2-
-------
•->
Oregon Method 7 Sampling Data Sheet
Stove Name H@ Date c3-'G> -"O I
Train Operators
Run # l(}fS"
2S^
3<\<\
Pressure
Nozzle Diameter
Meter
Vol
s^e-n
«S5Hl
5F«76/
Pi tnt
AP
x OO^-i
'OCTM
;.';'/•/•'.
• ]-,'
Orifice AH
Calc.
Act.
.IZ
»\2-
'/ ,' -
,' '
Stack
Ts
SLSA
c23G
6-7V-7
"
Gas Meter
T in
T out
H^
^6
ii'.: •
->
Vac.
0
0
Rny T
An
^9|
Temperatures
Imp.
76
3O
WB
DB
Comments
Qos ^"-7^ (2
3yj6
-------
Stove Name
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase #
_r
Box
Clock Times (24 H)
CONDENSED WATER DETERMINATION
Impinger: #1
Final Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
n
SV/.2.
#3
#4
c.<\
wz e_
Cf.L
Front Filter-First Filter #
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/ Front Filter Wash
Impinger Wash
Blank
Back Filter-First Filter #
Back Filter-Second Filter #
CREOSOTE COUPONS
Plate Location
/?}, 3$ c •/» g
Plate Identification
//j
Taj^e
Date
Date
Mg
Final
Net
.0/02.
/o,2
Total
Condensate
Plate Location
Plate Identification /Q
-------
Stove Name
Run # /7)
Box ff -2.
Oregon Method 7 Sample Recovery Data Sheet
Date
Phase #
CONDENSED WATER DETERMINATION
#1
Impinger:
Final Weight
Initial Weight
Net Weight
FILTER IDENTIFICATIONS
Front Filter-First Filter #
Front Filter-Second Filter #
WASH IDENTIFICATION
Probe/Front Filter Wash
Impinger Wash
Blank
CREOSOTE COUPONS
Plate Location
Clock Times (24 H)
Back Filter-First Filter #
Back Filter-Second Filter i
77)^
Plate Location
Total
Condensate
V-
-------
Laboratory Total Particulate Calculations
Stove Name . ^SA^1 _ Date of Sampling
Run # /d Phase # ~- / _ Date of Analysis
Box # j»_ I Analyst
I. Rinse & brushings of nozzle, probe, and pre-filter glassware.
Evaporation of. (R3 (ml) of
Final>?.-2-'£? (mg) - Tare
_
- Blank ( (. .poq mg/ml)(. /£3 ml ) = //^6 mg ) =
mg
II. Filter catch(es).
Front filter Final g.r*73 (X»g) - Tarep. V6?Mfrg) o,o*r$-(
Back-up filter Final/?. ^2.73 fag) - Tare.^. 2tf§y (mg) =
III. Hydrocarbon obtained by solvent extraction of water in
in impingers and bubblers.
Solvent used O.-&2, ~
IV. Particulate from evaporation of water in impinger and
bubblers following extraction.
Final 73. t'ji 7 ( ma , _ Tare 7£.£?^^g ) '^^ /2^. /
- J3lank ((_.oQ(t> mg/ml )( T^^ ml total
ml condensed =. 2^>V.^ ml) = /.2.;iy£mg)
Acetone Final
=
(mg)
mg/
Methylene chloride Final
= me/
Water Final
=
Other Final
=
.(mg) -
mg/
(mg) -
mg/
- Tare
ml ="'
(mg)
mi =
Tare
ml =
Tare
ml =
(mg)
mg/ml
- Tare
mg/rr. "'
(mg)
mg/ml
(mg)
mg/ml
Final 72 .j.f»2. (ing) - Tare z^Trf p(h?g)
- Blank! I .goa^r mg/ml ) (^ g^ .ml) = . . Z;zjS"mg) = 3-iq.il mg
Particulate from solvent rinse of impinger, bubblers,
and post- filter glassware. p
Solvent used .A-jfyAn^ ^ -2-33 .^
Final ?^. rr^ (gg " - Tare^/«$ f3 .(h>g ) *«--r /P^-^ r
- Blank (( .ooq mg/ml )( z.33 ml) = .2.10 mg) =J$2-2- mg
VI. Other particulate catches. =_, mg
VII. lotal particulate = H-IH-III-HV+V+VI =_j£££J£Lmg
Blanks
(mg)
-------
Laboratory Total Particulate Calculations
Stove Name ^d^ - Date of Sampl ing
Run
Phase # 2 _ Date of Analysis
Box # 7 Ana^st
" ' *v
I. Rinse & brushings of nozzle, probe, and pre-filter glassware
Evaporation of. \\'-j .(ml)
Final ?/. V^-(ttg) - Tare 7 A. V9-./ "fog) ^T? •'-'-'
- Blank (( .00^ mg/ml )(. iVc, ml) = I.Z.-Z-H
II. Filter catch(es). Fff g'7? 3£. **•*• .
Front filter ' Final_g>. g) e.
_ .
Back-up filter Finals. 3r^j (^g) - Tare C.^IY
0.
III. Hydrocarbon obtained by solvent extraction of water in
in impingers and bubblers. x?
Solvent used C.y»^ g-/- <2-~ ^r*K
Final 73.*(,6i. (iqg) - Tare?-*-??'?/ fag) ^e-T ^ ^/- f \ks) - TareTg. f^?9_Cipg) -»ii-r -2^7 2. ^/
(( >oo<=. me/ml) (_ zZ>G ml total
. g ml condensed = .^gfc. "2. ml ) =/.237mg) » 23%te mg
VI. Other particulate catches. -t mg
VII. lotal particulate = I+II-HII+IV+V+VI
Blanks
(mg)
-------
FLUE GAS EXHAUST PLUME EVALUATION FORM
'Time
-
)
0
-
- -
'.-~O
^ /:"
"O
YO
3O
,4"
1^
PO
"30
1 j—
;£-
/ ">
;4"
//"
QO
/O
_ /-
lG
"S^
•so
oc
_ i_
A -S
A.-T
-0
P3
^_
I S
/r
1/4
-
--r-
n,~)
o, O
36
"3.O
Of)
-:xO
PO
-V5
,/--
I -;
."O
/6"
nQ
po
20
PO
^
~}- *~>
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Date vv." - -'
Clock Times ('24 H) '." -:' -i"
Run # |o
Phase # ^L-
Observer ^ .-",-, , "'•'iv
Distance to Source ^~r,
Direction to Source -S" ^
Wind Direction JE?
Wind Velocity o --S"~
Cloud Cover 'T'O 'p-.
Plume Background ~'-> -.-.; r ^,,
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No. of Readings % Opacity
0
10
20
30
A n
40
50
60
60+
Units No.
Minutes of Observation
^zT'-.-v;
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FLUE GAS EXHAUST PLUME EVALUATION FORM
Time
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Stove Name
Date ' . .
Clock Times (24 H) ;' "-
Run # ^ Bi-
phase # 2_
Observer -, • i; , J."
Distance to Source 7>.^
nirprtion to Source c- i-
Wind Direction ^ - -. TL-^-O. /A-p
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Relative Humidity
A-v
Type Contaminant '- v--c/;--^ ,^''-^/
-------
Bacharach Smoke Spot
Run
Date
, ,-s / Operator ^-\
Test Time
Number (24 H Elapi
Sample
..
Location
--•
Temp.
r
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Spot
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Value
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6
3_
Test Time Sample Temp. S
Number (24 H Elap) Location Va
Comments :
e d
-------
l/J •'
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-------
ORSAT DATA
Stove Name
Run #
Phase # ,
Sample Time
Accumulative
Net
Sample Time f^- \ ^
C02 02 CO N2
Sample Time
Accumulate
Net
Sample Time
Accumulate
Net
Sample Time
Accumul ate
Net
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CO
co
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C02 02 CO N2
C02 02 CO N2
Date
Operator
-------
ORSAT DATA
Stove Name ; Date
Run # / "7
Accumulative
Net
Sample Time
Accumulate
C02 02 CO
C02 02 CO
Accumulate <, • ^ [•/,:' J j. j
Net \.^ If ^. f
Sample -Time \
C02 02 CO
Accumulate _^_
Net _M
Sample Time *3> 1*1;
C02 02 CO
Net _±^L /_!
Sample Time
Accumulate
Net
.-'• /-
C02 02 CO
-------
Moisture Data
Stove Name
Run #
Phase #
Date
Operator
Time (24 H)
1/14-
i4
Temperature
Wet Bulb Dry Bulb
\1(
. 2if
Moisture
Percent
C KMtv^'i -fo
>
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-------
Wood Moisture
Date ({ - ^ S
Operator ~ 0.'.
FUEL
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2 y '
3 ^^
4 ^ /
5 N
Dieter Me
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26
2*
24
21
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Total Mass (Dry Basis)
-------
Run
Stove Name
Operating Parameters
Clock Time (24 H) /&!£
Operator
Fuel : Initial Charge (ib)
Test Charge
Remaining Coal Bed (Ib) ^ / (Ib)
>; Kindling ^,,^J pieces J/t & lb
Comments
(Footnotes)
Comment Number:
VI
-------
-*%/_ w'
L
ftun * _/Z Date _^AAlL
Stove Name
Operating Parameters
Clock Time (24 H)
Operator
Fuel : initial Charge (lb)
Test Charyc.- . pieces
Remaining Coal Bed (lb)'
lb; Kindling pieces lb
Comment Number-
CftT. Tew d £J-7 $ <&£>">»• ^ y*o- *> /»if>s<>f'^/y stefa/.«{ Tf
-------
pa.
Run
-U-
Date
Operating Parameter^
Clock Time (24 H) __
Operator
Stove Name
Fuel: Initial Charge (Ib)
lest Charge pieces
Remaining Coal Bed (Ib)
Ib; Kindling pieces Ib
Hasped
Time
•linutes
Fuel
Weight
Ibs
TEMPERATURES <9>z_
Combustion
Air
Combustion
Chamber
Stove
Surface
-OjHteHy
Meter
Catalyst
Pre Post
NDIR
CO
C0
HC
ppm
Opacity
Comments
( Footnotes)
.IS
HSb
/to
77
7.7
T^L
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7ZL
ttl
/S,S
222
70
J
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10.
m.
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2ZZ
jaz
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(4,0
Comment Number:
330
no
32o
.7,1
3/6
.75
tb.O
7*7
?• TV
-------
Run .'/ _/y Date
Operating Parameters
Clock Time (24 H)
Operator
Stove Name
X X
Fuel : Initial Charge (Ib)
Test Charge
Elasped
Time
Minutes
'30$-
210
3-1. <
JL£\
&4L
Fuel
Weight
Ibs
3*7
3, /
^2^L
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2
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43
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Stove
Surface
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Opacity
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JLf&
,
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Comments
( Footnotes)
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dvfy jfgsJ
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Pw@ W^y
Comment Number: