United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park NC 27711
EMB Report
Nov 1989
VOLUME II
Air
EPA
Woodheater Test Method
Fuel Comparison Study at
Higher Elevations
Emissions Test
Report
Crested Butte
Colorado
-------
WOODSTOVE TEST METHOD
AND FUEL COMPARISON STUDY
EPA METHOD 5G vs VPI
MODIFIED EPA METHOD 28 vs CORDWOOD
RTP, NORTH CAROLINA AND CRESTED BUTTE, COLORADO
1989
EPA CONTRACT NO. 68D90055
SUBCONTRACT NO. 2-89-0055
PREPARED FOR:
DENNIS HOLZSCHUH
U.S. ENVIRONMENTAL PROTECTION AGENCY
EMISSIONS MEASUREMENT BRANCH
RESEARCH TRIANGLE PARK, NC 27711
PREPARED BY:
ENGINEERING-SCIENCE, INC.
ONE HARRISON PARK
SUITE 305
401 HARRISON OAKS BLVD.
CARY,NC 27513
May 18,1990
-------
TABLE OF CONTENTS
Table # Title Page
1.0 Introduction 1-1
2.0 Summary and Discussion of Results 2-1
3.0 Test Facilities and Methods 3-1
4.0 Wood Stove Specific Information 4-1
5.0 Appendices
Appendix
A VPI Method - Sampler Operation and Procedures A-l
B Equipment QA/QC and Calibration B-l
C VPI Gas Analysis Results C-l
D Sample Blanks D-l
E Graph Values and Formulas E-l
F Proportionality Data and All Raw Run Data F-l
For Each AK-18 Test at Research Triangle Park
G Proportionality Data and All Raw Run Data G-l
For Each CC-150 Test Conducted in ES Wood
Stove Lab
H Proportionality Data and All Raw Run Data H-l
For The AK-18 Tests at Crested Butte
I Proportionality Data and All Raw Run Data 1-1
For The AK-18 Tests at Crested Butte
J Proportionality Data and All Raw Run Data J-l
For The S-173E Tests at Crested Butte
K Proportionality Data and All Raw Run Data K-l
For The Ashley Oval Tests at Crested Butte
WS\RD123.40
RJM1371A.LOT
-------
APPENDIX H
PROPORTIONALITY DATA AND ALL RAW RUN DATA
FOR THE CC-150 TESTS AT CRESTED BUTTE
-------
TEST SERIES
A-l
IID123.40
1381AAPP
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
PC
I
Stv nanu: Orville
Model no: CC150
Lab name: ES/CB
1st date: 11-9-89
Run no : fl-1-1
Tst tine
(•in): 720.00
Chrg ut
(Ib uet): 27.40
run
time
Uin)
0
60
120
1BO
210
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.052 .
0.054
0.055
0.056
0.054
0.054
0.054
0.055
0.054
0.054
0.052
0.053
0.054
Units l=metric,
2-English:
Y, DGH:
Pilot co:
Gas MW :
Pb (MI, in. Hg):
Stack area («2,ft2):
Wood moist (?. uet):
Burn
stack
temp
(C,F)
59
87
92
94
99
99
90
87
88
80
87
86
80
DGM
rdg
(m3,ft3)
992.000
1022.400
1053.700
1085.600
1117.500
1149.400
1181.300
1213.300
1245.100
1276.900
1308.700
1340.200
1371.702
DGM
temp
(C.F)
58
71
90
96
97
99
94
91
89
85
88
91
84
Samp vol
2 (sm3,scf)
0.995 266.047
0.99
28.56 Flou rate
21.80 (dsm3m,dscf.i>)
0.1963 146.46
10.59
rate (dry kg/hr): 0.93
DGH dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(Ft/min)
1057.26
1106.08
1121.36
1133.56
1118.14
1118.14
1109.10
1116.27
1107.09
1098.98
1085.40
1094.78
1098.98
PR
<.'/.)
106.
102.
100.
98.
100.
98.
99.
99.
98.
101.
101.
98.
1
8
2
9
I
1
6
0
8
5
1
6
dOGM
vol std
(«3,ft3)
22.506
22.605
22.243
22.003
21.963
21.885
22.151
22. 133
22.213
22.376
22.044
21.925
85.49
17.640
460.00
1850.00
vs/VmTs vs ave stack DGH
ave temp ave temp
(C.F) (C.F)
. 0.01 1105.01 86.77 87.15
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
10
Stv nanu: Orville
Model no: CC150
Lab name: ES/CB
1st date: 11-10-89
Run no : fl-1-2
1st time
(»in): 720.00
Chrg ut
(Ib uet): 22.20
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.050
0.050
0.048
0.045
0.056
0.045
0.050
0.052
0.054
0.053
0.053
0.053
0.050
Units l=metric,
2-English:
Y, OGH:
Pilot co:
Gas MH :
Pb (mm, in. Hg):
Tunnel area (m2,ft2)
Hood moist C/. uet):
Burn
tunnel
temp
(C,F)
65
72
79
76
75
74
70
73
70
72
70
72
70
OGH
rdg
(m3,
373.
404.
435.
467.
499.
531.
563.
594.
625.
657.
688.
720.
751.
ft3)
400
200
900
800
700
600
200
500
800
200
600
000
462
DGI1
temp
(C.F)
78
91
102
100
96
93
88
90
88
87
87
87
87
Samp vol
2 (sm3,scf)
0.995 263.576
0.99
28.56 Flou rate
21.82 (dsn.Sm.dscfm)
0.1963 143.93
11.01
rate (dry kg/hr): 0.75
DGM dH
(mm
H20)
(in.H20)
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/min)
1042.22
1049.15
1034.69
999.04
1113.44
997.18
1047.17
1070.93
1088.25
1080.16
1078.13
1000.16
1047.17
PR
(X)
101.3
102.5
102.0
105.8
95.4
105.3
100.8
97.7
97.1
97.7
93.2
97.9
dDGrt
vol std
U3,ft3)
21.975
22.083
21.788
21.865
22.023
21.934
21.924
21.844
21.994
22.034
22.034
22.078
85.49
17.640
460.00
1850.00
vsA*mTs vs ave tunnel DGM
ave teitip ave temp
(C,F) (C,F)
0.01 1055.98 72.15 90.31
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
EC
I
Stv inanu: Orville
llodel no:' CC150
Lab name: ES/CB
1st date: 11-11-89
Run no : fl-1-3
Tst time
(min): 720.00
Chrg ut
(Ib uet): 17.10
run
tine
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.045
• 0.049
0.048
0.047
0.047
0.048
0.048
0.048
0.048
0.048
0.048
0.046
0.046
Units l=oietric,
2=English:
Y. DGH:
Pi tot co:
Gas MU :
Pb (dim, in. Hg):.
Tunnel area (m2,ft2)
Mood moist (.'/. uet):
Burn
tunnel
temp
(C,F)
78
83
87
85
84
80
91
89
83
81
84
84
86
OGH
rdg
(m3,ft3)
752.305
783.000
814.100
845.400
877.000
908.800
939.800
971.300
1003.000
1034.600
1066. 100
1097.300
1128.971
DGH
temp
(C,F)
78
82
90
91
91
84
89
93
88
83
88
93
94
Samp vol
2 (sm3,scf)
0.995 263.592
0.99
28.56 Flou rate
21.78 (dsmSm.dscfm)
0.1963 137.54
13.39
rate (dry kg/hr): 0.56
DGH dH
(am
(in.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
0.670
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
vel
(m/snin)
(ft/min)
1001.82
1050.25
1043.30
1030.48
1029.54
1036.60
1047. 10
1045.20
1039.48
1037.56
1040.43
1018.53
1020.40
PR
(.'/.)
102.
99.
98.
100.
5
0
5
3
100.3
100.
99.
98.
99.
100.
98.
101.
4
7
7
4
8
6
7
dOGH
vol std
(m3,ft3)
21.860
21.985
21.804
21.973
22.112
21.834
21.984
21. 963
22.094
22.227
21.814
21.943
85.49
17.640
460.00
1850.00
vs/VmTs vs ave stack DGM
ave temp ave temp
(C,F) (C,F)
0.01 1033.90 84.23 88.00
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: Orville
Model no: CC150
Lab name: ES/C8
1st date: 11-12-89
Run no : R-l-4
1st time
(«in): 720.00
Chrg ut
(Ib uet): 13.50
run
time
(inin)
0
60
120
1BO
240
300
360
420
480
540
600
660
720
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
• 0.
0.
0.
0.
0.
0.
dp
H20)
H20)
045
045
046
046
047
045
045
043
045
043
044
043
043
Units l-«\9tric,
2=English:
Y, DGM:
Pi tot co:
Gas MM :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Wood moist (?. uet):
Burn
tunnel
temp
(C,F)
92
87
90
86
82
77
81
87
83
81
79
80
84
(m3
131
162
194
225
257
289
320
352
384
415
447
478
510
DGM
rdg
,ft3)
.803
.800
.200
.600
.600
.000
.400
.100
.000
.800
.100
.500
.327
DGM
temp
(C,F)
80
83
69
94
92
85
83
90
90
87
86
85
91
Samp vol
2 (smS.scF)
0.995 264.167
0.99
28.56 Flou rate
21.70 (dsm3m,dscf<«)
0.1963 134.75
9.67
rate (dry kg/hr): 0.46
DGM dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel-
(m/ain)
(Ft/min)
1016.64
1012.03
1026.01
1022.28
1029.54
1002.74
1006.46
989.28
1008.32
983.84
993.38
982.93
986.57
PR
CO
100.0
101.8
98.6
99.2
96.1
100,7
102.8
103.1
100.5
101.6
101.3
104.7
dOGM
vol std
(m3,ft3)
71.913
22.075
21.834
22.050
21.715
21.994
22.286
22.141
22.071
21.844
21.953
22.293
85.49
17.640
460.00
1850.00
vs/VraTs vs ave tunnc DGM
ave temp ave temp
(C,F) (C,F)
0.01 1004.62 77.79 87.31
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
Ln
Stv manu: Orville
Model no: CC150
Lab name: ES/CB
1st date: 11-13-89
Run no : fl-1-5
1st time
(min): 720.00
Chrg ot
(Ib uet): 21.30
run
time
(min)
0
60
120
180
240
300
360
420
480
510
600
660
720
vel dp
(nun H20)
(in.H20)
0.012
0.043
0.043
0.042
0.042
0.045
0.044
0.045
0.043
0.042
0.043
0.042
0.042
Units l=nietric,
2-Engli5h:
V, 0611:
Pilot co:
Gas MM :
Pb (mm,,in. Hg):
Tunnel area (m2,ft2):
Hood moist ('/. uet):
Burn
tunnel
temp
(C.F)
7B
76
60
71
92
87
83
79
82
89
84
95
98
OGI1
rdg
(m3,ft3)
511.814
542.800
574.400
605.700
636.700
668.000
699.900
731.700
763.200
794.800
828.800
858.700
889.727
OGM
temp
(C,F)
79
84
89
82
91
91
88
85
83
36
90
89
90
Samp vol
2 (Slr»3,scf)
0.995 263.304
0.99
28.56 Flou rate
21.64 (dsi»3m,dscfm)
0.1963 131.95
10.97
rate (dry kg/hr): 0.72
DGH dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
6rt)
670
670
670
670
670
670
670
670
670
670
670
670
vel
U/min)
(ft/min)
970.98
980.64
984.29
964.64
983.53
1013.43
998.44
1005.99
986.12
980.86
987.93
986.20
988.86
PR
(?.)
101.
101.
97.
104.
100.
98.
99.
99.
103.
109.
97.
101.
0
8
9
2
5
7
7
1
1
9
2
8
85.49
17.640
460.00
1850.00
dDGM
vol std vs/VmTs
(m3,ft3)
21.885 0.01
22.113
21.704
21.774
21.625
22.040
22.091
22.003
22. 154
23.706
20.695
21.515
vs ave tunnel DGN
ave temp ave temp
(C,F) (C,F)
987.07 78.14 86.69
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: Orville
Model no: CC150
Lab name: ES/CB
1st date: 11-14-89
Run no : fl-1-6
1st time
(min): 720.00
Chrg ut
(Ib uet): 25.30
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.044
0.044
0.045
0.045
0.045
0.044
0.046
0.042
0.042
0.043
0.043
0.042
0.043
Units l=metric,
2=English:
Y, OGM:
Pi tot co:
Gas MU :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Hood moist (.?. uet):
Burn
tunnel
temp
(C,F)
85
92
99
92
91
79
76
87
%
92
85
89
82
DGM
rdg
U3,ft3)
890.408
921.500
953.300
985.500
1017.400
1049.300
1081.100
1112.600
1145.900
1177.200
1209.400
1241.600
1273.604
DGM
temp
(C.F)
68
85
90
92
94
87
82
84
96
98
92
94
93
Samp vol
2 (sm3,scf)
0.995 264.781
0.99
28.56 Flou rate
21.53 (dsn.3m,dscrm)
0.1963 132.36
12.41
rate (dry kg/hr): 0.84
OGM dll
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1120)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/ain)
(ft/min)
1002.83
1009.24
1027.10
1020.65
1019.72
997.29
1016.86
981.56
989.61
997.71
991.36
983.36
988.63
PR
(.?.
102
102
99
99
96
99
99
109
99
100
102
101
)
.9
.6
.9
.0
.6
.2
.9
.4
.7
.1
.6
.?
dOGM
vol std
(m3,ft3)
22.304
22.100
22.174
21.888
21.809
22.019
22. 152
23.046
21.322
21.856
22.094
22.017
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave tea
(C,F) (C.F)
0.01 1001.99 81.79 88.85
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
II .1.
1 0 • ^
^rrr^
DATE DEPLOYED //' . *? - 'b' "l
DATE RETRIEVED I/ - J cf- 9 Cf
TEST LOCATION C Sr")77 (MIN. )
STOVE ID £ C / 6 &
WOOD SPECIES
WOOD MOISTURE (Z DRY) / Z., 5 1
WOOD MOISTURE (.7. WET)
WOOD CONSUMED (LB)/Z£-.8 (KG) 5 7
SAMPLE FLOW RATE PRETEST
TANK //. cj $ (—IN HG) TEMP. /
(C)
TORR ABSOLUTE
POSTTEST
ROTAMETER_41__= (ML MIN)
PRETEST LEAK CHECK
START
(IN H30) FINAL_
_(IN H20) LEAK RATE Q , I (IN H20 MIN)
POSTTEST LEAK CHECK
START j^,^ (IN H20) FINAL
(IN K2) LEAK RATE O ,
(IN H20 MIN)
POSTTEST CAS ANALYSIS
RUN COMMENTS:
CO(Z)
/'
02(Z)
GRAMS MASS ArTER FLOWING O.S 1pm NITROGEN FOR INDICATED TIME
PRETEST
lac
PROBE+FITTIN3 7 .
SAMPLE LINE
CONNECTOR
MIN.
MJN. + MIN.
MIN.
DELTA
-o-
H-A-1-7
-------
Pair a
/of _ /
CLIENT
PARTICIPATE WEIGHTS SUMMARY
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ES PROJECT l\ 0 IZ 3 STOVE MODEL No.
POSTEST
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WT 3
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FINAL WT
TARE WT
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DATE /TIME
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-------
PARTICULATE WEIGHTS SUMMARY
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STOVE MODEL Mo.
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Acetone Lot II.
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-------
CLIENT
PARTICULAR WEIGHTS SUMMARY Pacfe / o£__/_
RUN No. *>& /) / Placed in Dessicator: Date/Tiine_/#Ll
ES PROJECT R 0 )?-'3 STOVE MODEL Mo. C-C - /
POSTEST
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Acetone Sample Volume_/_
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,
7 9/^^/2.
' 7-/.^ //u-
. o 6 9£
CALIBHATIOH HT
VIT AMOUNT -
PRE WT
So , WUt)
SO , O&QO
POST WT
5
-------
PARTICULATE WEIGHTS SUMMARY
Pa (jo.
/ of /
CLIENT .
ES PROJECT
RUN Ho..57- /?-/-/ Placed in DessicaioiN Daha/']'ima //-Q-S'<( ^23.$o
STOVE MODEL Ho. f C - / ^r>
POSTEST
>
• WT 1
WT 2
WT 3
WT A
FINAL WT
TARE WT
WT GAINED
DATE /TIME
l<*6o /////
/-// (&10IO
//~*/-**>c/
FRONT
li-Tr.TRH II
Z-72. /
A/92.7
/./937
^•/f37
• 6 So 7.
. 5/35
DACK
FTr.TKR I!
-2 7 S
.<;?r/^
^g'Z.T-
• 68'i2_
.'/7-/y
.ovlt
CAHURATION WT.
WT AMOUNT =
PRE WT
( *>OOO
* ^occi
POST WT
. £c,0o
*V?
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Pago / of
RUN No. ^C--/)-/-1- Placed in Dessicator: Date/Time.
21 3o
ES PROJECT K £> /23 STOVE MODEL No. CC-/5b
POSTEST
'
' WT 1
HT 2
NT 3
HT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
//-// & u$o
It-f/-^) l(^^
.<^Z53
DACIC
FILTHR II
^4T01-
, c-^v^
.6937
«
, ^?37
.68Z/
•
i
>—•
i
(A)
(13)
-------
I
t—•
I
t—•
CO
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY PageJ_2 of_/.
RUN No. 5<£'//?"'/~ 3 Placed in Dessicator: Date/Time//-^ S"?
STOVE MODEL Ho. f-C - /^
POSTEST
1
• WT 1
WT 2
WT 3
i
WT .4
i
FINAL WT
i
TARE WT
WT jGAlNED
DATE /TIME
/*•)
//-/t-fr'/yVo
l/-/lQ HIS
/(-3-V1
FRONT
FTf.TF.R IL
^-77
/.3/VZ-
1^)51
1.3/S/
. 6#oZ.
.tzy?
BACK
FTI.TKR II
/^-:7^
•^W
.m$
.6,34,*
*6>-?.16
.&V79
GAL JURAT ION WT.
WT AMOUNT =
PRE WT
. 5
-------
PARTICULATli: HEIGHTS SUMMARY
Pa [jo.
/ of
CLIENT .
ES PROJECT
HUM No. ^>-/?-/-V Placed in Uess icator: Date/Time //- /2-fll
STOVE MODEL Mo. C-^ ~ / ^
POSTEST
;
' WT 1
WT 2
WT 3
NT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
<7-/3 (9/Ao
//-/?& /v ^^
//./yC^/8/6
//- 3-^^
FRONT
p-Tf.TF.n II
/}£-<6^
1-^0^
/.OS9/
l.cQo*
I* o^oV
.67/2.
^k
DACK
KTf.TKn II
n^-^
-476 ^ <^rO
'^^cvr.
.^737
.O.M
CALIDHATIOM WT.
WT AMOUNT ~
PRE WT
, f^,/
r 5'frz-fj
^ 6"6C^'
POST WT
. 5<^/
•? '^t'Jjrri
, W)
nOOH CONIHTIOMS
RELATIVE
HUMIDITY
•zz^<£7
/^<^^7
-21^67 •
UAKOHTUC
PRESSURE
•z/.?
2/>6
2/^ •
Initials
,
/^&/l
W/l
/^Of
(A)
(B)
-------
CLIENT .
ES PROJECT
PARTICULAR WEIGHTS SUMMARY
FfeT/4 - /~ 5" . Placed in Dessicator:
of_ L
Date/Time l)
STOVE MODEL Ho.
POSTEST
'
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
H-iH ($lSif
U-/Y& 1%-W
//~/S& ft^5
//-•s-z*
FRONT
FTF.TRO II
y)/r-75
I.H 99 7
fcloo
* 6*700
^ (sIc'-O
.£^0
,tUG
CALIBRATION WT.
WT AMOUNT =
PRE WT
.. 5<:^^
.-vm
<^9£T>
^ 5^r'^»
j ^C'C'O
ROOM CONDITIONS
RELATIVE
HUMIDITY
/V6>67
-z 2^, 7
7.^(><, 5
BAROMTRC
PRESSURE
t/f cf
-L/.&
T-/-^
Initials
t
/*f^/?
/?->^/7
rt\c/^
•
(A)
(13)
-------
PC
I
CLIENT /
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY
0^-l
* S^1^^
POST WT
<; ^ ^//i ^
x 6 C>fO
* ^CrZ'-t'
ROOH CONDITIONS
lUCLATIVE
HUMIDITY
Z"^},?
2/^7
7. / ^ 7
13AROHTRC
PRESSURE
-£/.
-------
Client __
Date U-'V%C"\
WOOD HEATER CERTIFICATION TEST INFORMATION
Run / ; • A'- I -
ES Project f
"Wood Heater Model CC/5O
Operators. UoVU4 . .\ MelAv
TEST RUN INFORMATION
Attempted Burn Rate (Kg/nr) _ Secondary Air Setting
Achieved Burn. Rate (Kg/hr) .^Z.G J Thermostat Setting
Other Settings
Primary Air Setting
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
•2j. e
'xfc
5~
/C'.-C--/l',<:
5r»
o.co i
Post Tesi
2. /. S- •
6 T
<5
^9
/•?,f - 4, o
? /*y
,
TEST FUEL DATA
I.SL.
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Actual Fuel Charge Wt. 7.1.
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20t Dry
£-7
-------
/H-/
HOOD IIEATEU CEUTIIMCATIOII TEST
IE
flr~r
VWn.
Vtonil
ENGINEER
Client
Date y
TEHPEIIATUUE AMU I:UEL COMSUMPTIOH
iHG-SCIENCE, INC.
/rp/} Run j /-)- / • 1 Test Fuel
/- 9~ ^ *•") Mood Heater Model CC-/"?^ Coal Dcd
ES Project I
Time
Sampling/
Clock
09V/
f ' 9 *) 'n
//? "2 ^
/£.' '/ -"*:>
// o /
// o '2_
// ^0
/I *;/?
/ ?
~Ln GO
-> / To
Test
ruel
n.
(Ibs)
f} t()
1 . t
"? ^?
c^ ,/
flL*-*^^
uif"7
t/,1/
C **<^
V^9
"9,, 5
/fit1!
*-f,"L
-^7
n
BftX^J
• oyo
, (.'Ljt,
.0^/6
. o"y/^
L1"1)^
t^^tj
..' ^;
tli\O
•A'£&
p--i>^
. Z>'«, L
JLti/23 Operators /#^ ^J /^
Comments
iTc /(•/ c'V/}s7~
K /A/ (V £ /AX. .x.^ A//1f'/'
SI r/rt"&~l,f k^*r// ,,',.,-'
?.i.l ^ "3» / *> ^/j '<^>,^.C/
' / /
V4 ,^7///,v "^ V^V •"*•
VjTx^r.v ~ /.» ,3 ^
<-/e~L- y)*1^ •» 3 - "J 'l'rr'
Vi'/ /'/?>»*»' r "5'^ ^
> , 9x^x. T- •*• 7 « 3 <^
P*nhf\f.t /]if. y-"L- > / r "7* t/ "^
Fii / /*A rt /• j, /*) ; ^< / C Xt
A7A- -frt..//., Os>t"J
Combust or Temp.
•C V
^7
^77
^v' 7
'"2.£:'
cj(7^S'
c
. *V7 ^
UATA SHEET
Cliarye
Surface Temp.
lop
/h&
•TV
//3
?^7
?'v?
y/v
TL?Q
7^7
^3
^%
^2
Zfc'2.
^/•3
?<&'/
-j/^
llenr
Uottom
•
Hi gilt
Left
Page / of
Stack
Temp .
^••
^,- 7
"2/*y
y^v
yyz.
V5Z
V6*?
V7v
T y<7
7. ^."7
2 ""•5C/
y "J'S'
3^^
"?^S
i?s-
Oil,,
Tun.
Temp .
5^9
M
«g"7r
-
loom.
Temp.
< T
•99
-?
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date //. c)
SAMPLING-DATA
A
Sampling Location^',
Sample Type
Run Number_
Operate r^y
Ambient Temperature
Barometric Pressure
Static Pressure, (Pjl
Filter Number(s)
Meter /lA.T 1 f> n G
In ls>
•^o
t^i-
f f, I Q <7f7
~>C //o<
' cjo if 2r,
)&
/•mtf / 7
JL°
?T
/ ti t> IT^^c,
/<} T f*>
9 1 c 1 '
0 V
1o
1. L/0 fT} °iO
Z TT /'t-/t>ci
Z 1 o lH2X^
^gc, iqT.s
•T.OO i>-
^ / ^ / ^
r-?O
- t'
•^^D /^ 7«
o,«-/^ / 4" 3^
Gas Meter
Readi ng
(vm) ft3
qc/9.^
/V.> '2.Z 'j V
6<^ "3 .. • 7
,
tosr-f, 6
IHTi1:)
•
1 |v-/tj j_/
i/^/. 3
Velocity
Head
( PS). in.
tfO 1 "*-•
. t> r, \-
, e- ^ ~T-
vO 5 2.
»f><^ .. t. 7
(o, ^7
Actual
t'> .- /• 7
• /^7
.. "7
- ''"I
.G> ~7
' fc ~)
,.(. <-}
j 11 ">
,. 6 1
TEMPERATURES
Di lution
Tunnel
Me t e r
In
«7*^
6 3
-7 "^
9 v
9 S
,^'j
7V
•^ 3
Meter
Out
f;^
ifU
-1 /
c/o
96
Ji~7
c/ V
9V
Filter
*i 7
•
Impinger
^ ~L •
6"3 V/
7^
*> /
~) <% C7 v
?>/ ^9
&5 • ^c/
/?Co 5'2_
Sto 5"p
Pump
Vacuum
in. Hg
~2,
"^
3
'•?
3
^
1
Flue Draft
in. H20
tu
t
I
I—'
I
-------
rgpjai fr^Ti ^
»-:cn3 tj'.E^x
tf-nr-n Egrriv'J
ENGINEERING-SCIENCE, INC.
•IP LING DATA (cent.)
Vlood Heater Cc - /"5V.,
Date
Sampli
Sample
//- 9 - 8 '7
ng Location C'/' ,-'^<^:/ /5'<:>PT&
Type ^
(j- ^
/?-/-/
Hun Number /)-/-/
Operator /#^/\ Sf)/s
\. Clock Time
Sampl 1 ng\(2'l-hr
time, m1n\(;iock}
~3~£7>" — ~ J-S&L.
'*>'?*-} •//r(<£)
"WO /Mo
*£2.O 'JC-^O
>~l 35 _/:2_<^L.
V 5& /~)1o
^ (^ /•?'•? «7
V 5>o y ~2_
V 9 ? / b '•"?
^yr, /^^
5 V<9 1 ^ C;>
<"T^ l^c^
£7c> /9 2 <5
^fl'T /9 3"?
?:^& A/ 5i--
/ /<^r *7si/ £
61rj ?. o2o
faf-n 2o <)(<
fa 75" V y^*)"
/•,9£) 1 / '2o
"jot) ~i/ 3 5
Gas Hater
Readi nq
(vm) ft3
Ii7 ^-"-3
1 ""? ^V ^ /
V"7 "7^- ^~J
l"3t>'5»"?
[•^Vft, -z
Velocity
Head
Ul's) in.
lt?0
. o 5V
_ ^.^ 5y
< <> f> ^
fo^,<,
' O^t <>
e o^Y
. a 5~"^~
r f>*>'/
fC7 ^ Y
' '•> S3
/> o ^/^
o o S 2_
65 ^
. f "7 7_
.O>O
to'-iSi
oO'i ~L-
r f>'>1
a O S "•?
Ori f ice Pressure
Di f ferential
(All), -in. ll?0
Uesi red
Actual
. ^7
6 L~)
- (/ "7
* O' /
J O? /
« /-. "?
, t, ?
/ ->
, A 7
* & 9
•• ~?
fr">
•• 6 ~)
'
TEMPERATURES
Ui lut ion
Tunnel
Meter
In
<9 /
C6
q/
-
Meter
Out
°\ /
89
^ *>
3
">• *r
;>, 5"
-5.
-------
FUEL MEASUREMENTS
Date J/-''1~Ocf Hood Heater Manufacturer
Project No. £c, \ z."^ Hood" Heater Model c.c.i
Run No. A - I - ' I
Circle One: Pretest Fuel
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; .Actual Load Weight
Fuel Piece Length .
Moisture Meter Calibration -t25- ' -255- 3>/ Z /7S* Z.1.0
Moisture Content-(Meter - Dry Basis)- Cor/'KTtcL
Piece No. Readings Average
1 /Y_7_ _^f Itf
2 ^s° /.'.a n.c /
-------
Client
WOOD HEATER CERTIFICATION TEST INFORMATION
Run/ Ar-
Date l(\Ht>~&
ES Project
"Wood Heater Model
Operators ^~
O-C.
.\ Kr
TEST RUN INFORMATION"
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (8F)
Relative Humidity ('}
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft ~
Pretest
-zj.es
6-r
n
0>
it.o/jc.a
7. '-, <•-
NJ/V
Post Test
"2-X.g-V •
1o
/&
•9
((>*•//(>. C
^ /;• / '
Firebox Volume (ft-)
Fuel Charge Range Wt.
Actual Fuel Charge Wt. "Z
TEST FUEL DATA
Coal Bed Range Wt.
to Actual Coal Bed Wt.
t-1 "2— Fuel H2C£ Dry _M
Fuel: Dry Kg
to
Wet
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
B 1
2
3
4
Ave.
Pitot Leak Check
Static
-------
WOOD IIEATEU CEUT1RCATION TlTST
-_;
V~~jn
B«I|
W»oil
TEMPEIIATUKE AIIU FUEL CONSUMPTION
ENGINEERING-SCIENCE, INC.
Client lz P A Run 1 //-/- Z Test Fuel
DATA SHEET
Charge Page / of /
Date //- /o - 2>c} Hood Heater Model Cc-S^o Coal Bed
ES Project I
P3
1
1
i— •
1
N)
Time
Sampling/
Clock
Si
it uV
/2,O
1 {> trh
;.»'?
2-*?
z.v
£.6
V/'2-
"i- %
3. «y
•^ i
^ ' 'tf
£>'6
7>ri
5", ^
!?« £?
Fl.uc
Draft
(in
*: l>2<
VT.L;
a ti '4 *j
at'W
-><>.3?
tiVv
j.''"i7
*i>'t~l
i<2lp>
oil
*f£>
//oV 2.V/fr.V-= q.b'**
///£.' PS/hi*/*., 7?lr> nT / "
'
2, i7 / C( , /,, - T.. 9^rx7c/f^^/
/Q^ P/<^/)i/f/'i/ /9y/< F-* //.,&*>,•
, / , *
7
Combust or Temp.
'•y"2-"3
c> •? T
Cj Y C/
7/3 S'
7 9 7
G %O
*->' ~Z 7 •
Vf. ~7
Vt^A
V/7
T7 ^
38' 9
•/-
^y *r S'
1*3 Cj
fft-
^y
-?<^c,
V^t,
Oil.
Tun.
Temp .
75
^*7
9<^»
*7 'a'
9 '
95-
5" '7
§-^
V
70
^O
7-L.
7o
4-
7 2.
"7^
-------
ENGINEERING-SCIENCE, INC.
Wood Heater,
Date //- /
SAW LING DATA
Sampling Location
Sample Type ^'(^
Run Number
Operator
Start Time
Slop Time
< [7/-W
- / - Z.
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s) —jf
Meter ,
Probe Length and type jy •"
Pitot Tube Coefficient ..99
Assumed Moisture y
Sample Box Number /]
Meter Box Number ^/
Meter II A) A
/?
Pretest Leak Rate ^
Post Test Leak Rate
S>
19 \o,c,
lf)f, IWi
I'if) idbf)
/3<; {iff
1 ^0 ,)1,O
l ^c> V/V5
/Of /Z/"7
"2,/o /23o
1_'i,<7 /T.y'f
2 ^o / 3#v
^^ n/'i
\1fj /3V7
t.'^C. l2!*/^
^C-Y) / Yr/->
-2,,f^ IL//^'
-i-i ,,, -^ ,.,
Gas Meter
Readl ng
(vm) ft
37 3 - '/"£•
t/^V, -^
iy ^ 5, cj
'i(o~) '^
t/qy, 7
Ci-\l ,tf
Velocity
Head
( Ps).in-
H?0
a O C>O
a o "Jo
. f ) ^ Z.
« o 0 /
i o ^O
. o V O
, ('"Vii
'f^*^
* fj 3 1
. , o <-/6>
o'-l'l
, o Li ^
X y-^~l
y^J JjJ 'O
t C7?<<.
«* o 5"6
a 0CJ 1
-/ ( „
Ori ficc 'ressure
Differential
( H), in. H?0
Desi red
, o-y.s
Actual
> ^7
^ 6 7
^ A 7
/6 7
* //>7
^ 7
*L-~*
tr>~i
» Ct> 7
•> L>~>
.hi
tiol
& & 7
c &> T
i"f'7
r (.. 7
X ~1
> ^~>
, to~^
. t- ~7
TEMPERATURES
Di lution
Tunnel
Meter
In
•fto
Z
99
C\ fn
C/ 'i
Meter
Out
7 .^
^ V
9/
/ -t>
96
°) ^>
Filter
"7 "L.
Impinger
^ 1
7^ 5o
76/ 5/
<7,^ ^ <^
1?^ 5/
<_/ y-1 ^ T
i CA L-. i
Pump
Vacuum
1n . Hg
•^
-5
•^
••^
•^
-3
7
Flue Draft
1n. H20
-------
vresya
G£z3$
SAMPLING DATA (cont.)
Hood Heater CC
EC
I
I
NJ
ENGINEERING-SCIENpE, INC.
Date //- /£,- s-'v
Sampli
Sample
^/^
ng Location^v^^'Y^,r-/ ;3._l7&?
Type ^
,. • —
Run Number /?-/--?
Operator /^ <-& hi s/
• X. Clock Time
Samp11ngX(24-hr
time, minXCIock)
• ~ •— — — _
"V7S / Gi£
^9Q
H~*>5 /&AT"
H *>0 /£ 1o
t-i {^ ) 9 ^^
£)£? /^/^"
2.oV5"
Gas Mater
leading
5VY-^S
frl *i. ^
fa^li ~L-
S/ff.^, 6>
1 2&.o
Veloci ty
Head
.015 ~\
.OS'o
_j^5"2~
v o 5 "2
. 05-2-
tfO^'2-
^ n 5^
^ ^5 y
f o *> v
* o 5 Y
„ ,j 5 -^
» <3 ^ 3
* o •£ "i
*<>5 J
_.£><" "3
« » 5" "3
_^ ff"?^
ao*> '$
, o <;
, 05 '\
)ri fice Pressure
3i f ferential
(All), -in.
Dcsi red
e, -7
• L»V
-G7
IJ2.0
Actual
.G "7
.c*. -7
.6>7
-^ 7
.6-7
6 6* /
e 6>~1
r&>~?
* (0 / '
j
»
t>(t>~)
f<.,i
s.(j>~)
,,/„-)
,6*7
, ^,'-7
. /-, "7
.6-7
TEMPERATURES
Di lution
Tunnel
Meter
In
*7/
^i^
3-^
S? y'
c) 0
-
Muter
Out
^/6
^ 15T
sj-7
S"7
S 7
Filter
§O
77
'7 5^
7 S"
7 5^
Impinger
5-y
?"L
5-y
*5V
-
^-^
Pump
Vacuum
in. Hg
^
^
•5
-7
-5
Flue Draft
in. H?0
.
72 O ~L 1 ao 7 St V/T,2. 'O^'cy * (a") ^>*a ^^ ^ S" $"7 3
-------
M-2.
FUEL MEASUREMENTS
Date //-to "S°7 _ Wood Heater Manufacturer
_ _
Project No. f\.Q \ ~L.~^ Wood" Heater Model C<" . fS"O
Run No. A-- i — 2_
S-\V ^
Circle One: Pretest Fuel • <^festFug
Fuel Type and Amount 2x4 _ 4x4 — ; — 1x4
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length
_
Moisture Meter Calibration •&?_ _ _22^ _ Z-l> . ~
», =>. °F _ ^__ • •
Moisture Content-(Meter - Dry Basis)- Corv£c7c
-------
client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
........ Run I tf- /- "g.
ES Project t Rf) /2 3
"Wood Heater Model C.
/"*>'
£y
/<.>>£ - /<:• r>
/y/j
Post Test
Z/- "75 •
-7 Z-
'V
0
t& ,d /iO^O
.
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
to
Actual Fuel- Charge Wt. 11. (
Fuel H20i Dry l6W(a Wet /
Fuel: Dry Kg 6,7/6
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Velocity Traverse
Temp
_2fL
Ave.
Pitot Leak Check
Static
-------
ENGINEERING-SCIENCE, INC.
Client
WOOD IIEATEIl CEUTIF(CATION TEST
TEMPEUATUIIE AMU FUEL CONSUMPTIOII UATA SHEET
Test Fuel Charge
Page _/ of
Date //-//, ^ Wood Heater Model fC-/5c> Coal Dccl
ES Project. 1
Time
Sampling/
Clock
If) lf>
/r> y<3
// It)
'{~L / O
f 3 lo
/V 10
1 <->/&
Ifr/o
/*i lr>
\c\ \ o
~i.£> to
-z// 0
\
Test
:uel
n.
~2~,(f>
9*f
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T. /
^t'A
3j ^
3y~?
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7> L-
Cf1/
fa. o
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Fl.ue
Draft
,ftlo
vt'2.1
tO'Ll
• b 2. v
tfo/6
to'2.c,
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n^O'
](>!(,'
*rt/ 7
ort
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'
^, f) /2^ Operators /J/^/l iJ/y
Comments
'iT/l/'T
/?r7c/ ^^*
Pf^SM/lr v /?/" /-~>~// & PrfJ
' fill. //)i^ ftV 7c( / -/v "
/1><>5 cJ)..^?1t>A Mx'r-vi
.. -^n , ^ <-» r~H
/ / T y / ^ ^^ / / ^ S, ' "" / / (^ '^~~^
'
/6/T - /W/Vyv fake/ (?«/<,
Combust or Teinj) .
A/ 2-7
•9 '•? 4
7 ^9^
Y'^ T
-5*^y
T
~7 ~$
76~
d> ^*
^ 7
&Q
7'Z.
77,
-------
ENGINEERING-SCIENCE, INC.
Wood Heater CC
Date //- // - 9 <
SAMPLING DATA
/4-X-3
Sampling locatlon
Sample Type
Start Time
Stop Time
Run Number f\ - \- "*>
Operator
Probe Lenijth and type /*-/
Pi tot Tube Coefficient f. y<
Assumed Moisture
y
Ambient Temperature
Barometric Pressure
Static Pressure, (PjT
Filter Number(s) '_
Meter /
Sample Box Number
Meter Box Number /l/t,J~ff £,
Meter H SI'/£
Pretest Leak Rate ^
'Post Test Leak Ratfi,v
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
tlme.mln Clock)
<"> So So
J ' 1 25
1o *-/o
y*i <5"5"
Lo // /c
CjJ 0 ^~/C)
/ 9 *J 7 ^
2^ /O V^>
2ZT ^5
2 y/<^
T^S 2 <'
"2 yf yS^
••o4/ fr'
, ^ v ^
_.<7V •?;'
,. ^' '/ rV
Ori fice Pressure
Differential
( H), 1n.
Desired
II20
Actual
r <;- "7
t L?1
i fa 7
>7
•» 0) ^
< c^->
, ^- 7
, ^-, 2
^ 6- "7
-.6'?
i ^ "7
-c. 7
, 6-")
TEMPERATURES
Oi lution
Tunnel
•leter
In
T3
C1' ^/
Q -^
<7"Z
97.
"3 3
^rc//
Meter
Out
78
% Z
Vo
9/
9/
s-y
S7
Filter
-6r3 '?
•
Implnger
3 &~J •
7y •£" "^
79 ^
•
7 ?>• 5y
7y 5" "?
.S' 5 '
-------
SAMPLING DATA (cont.)
Vlood Heater C C
ENGINEERING-SCIENCE? INC.
Date //-//- y->
Sampling Location O'^rCvfY A'- 7^
Sample Type ^7 ,
^-
Run Number /-l'- / ~ ^
Operator /;, c/? /., | j/
X^ Clock Time
Sampl1ng\( 24-hr
time, min\v£lock)
:2T^>7> — • l-iJtii.
^7 /-?z f?
TV^J /o;^
^X^ /<57<
4" 7^1 yQVft
^7*i^7 /^7^5*~T
r ^t^ ^ (0 //?
/•/< -2/?2^
^'if> X^^(3
/(.Y'T ^^^
i-^V'7
^ v 7
.. ^' '•/ S
,. /i"'-/ V,"
x- 1 £-/ S>^
rf* *-' ' ^5
. c"-/ 'if
,oli ^
. c>'y '.j
, OLt ^
O'/ft
. ovti
,c y*-
. «y (f^
. oy-7
, ^7
j ^> <-/ (\
, f '/ r.-
3ri f ice Pressure
Oi f ferential
(ill), -in. ll?0
Ocsi i'cd
&'?
Actua 1
Y> ~l
,(, 7
/ 0^ /^
» c* "7
1 .- fa'/
/, '>
, /, "7
; /,•")
/
.-(<> "")
. L.I
. & 7
• &">
.Co 7
• o7
. C 7
.C, 7
,6 -7
,6 -7
,^ n
'<• 7
' "O
'
TEMPERATURES
Ji lut ion
Tunnel
1cter
In
c/ "5
ft' "7
2T3
C^*7
9V
Mu t e r
Out
^ 3
g -5--
^ 1
/jri
9 "5
•" i 1 1 e r
S'Z.
"7 "7
73
7 1?
-?">
Impinger
*r 5
So
5"c?
<5 /
^"^
'ump
Vacuum
in. Hg
••^
•^
T
-x,
7
Flue Draft
1n. H20
-------
FUEL MEASUREMENTS
A-l-3
Date
\\-~\\- &C1
Project No.
Run No. IX—i-
Wood Heater Manufacturer
Wood" Heater Model
Circle One: . Pretest Fuel •
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Height •
.Actual Load Weloht
Fuel Piece Length_
Moisture Meter Calibration
»Jvf(l r< «, ?. °F
Piece No.
1 6
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-CorVKTtcL
Readings Average
(7,5 2.6, S
(U_
(L! 131
Overall .Fuel Moisture Average
H-A-1-31
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' ' •' Run i 'A- I
ES Project t
\ 7-"b-
"Wood Heater Model
Operators (,\_ j^'H
N HcJ\
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr} A,I/6? 1 Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest | Post Test
2;.7ts
£7
;y
o
^f-i5 •
7o
>9-
0
;',.u/ ic.j 1 ''-':<-/ it. r,
1 1
,^-\ 1
TEST FUEL DATA
to
Actual Fuel Charge Wt.
'
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2Ci Dry
Fuel : Dry Kg
to
LOADING/TEST START OPERATIONS .
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
-------
flr~*
' *J—sft
I HtottlJ
ENGINEERING-SCIENCE, INC.'
Client /
WOOD IIEATEK CEHT1I:ICAT10M TEST
TEHI'EUATUUE AMI) FUEL CO||SUHI>T10H t)ATA SHEET
I /7 -/-
Test Fuel Charge
/3 S •
Date
Wood Heater Model CC - /5o Coal Bed
ES Project I R Q /Z 3 Operators Sh c A- t 7 7
£~yf
V-7 y
V^7.^
Vfr-
;'/•:-.
tt
132
27?
?^?
VT^
-v$
;-'.it-
^/"7
pz3Y
^f-{
S
Hear
ZT^
urfncc Tc
UoLtoin
inp.
ifghT
Left
•
Stack
Temp .
V5-T,
3/y
£W
2-^y
Z5:?
Z^S1
2cT
;
»y
*
^ooin.
Temp .
67
<^r
^9
7V
V^>
~?*s
70
7/
72_
~>
r,Y
A '9
-77
-------
ENGINEERING-SCIENCE, INC.
Hood Heater
Date //-//
SAMPLING DATA
/?-/-
Start Time
Stop Time
Sampling Locati on C
Sample Type <^ 6-
Run Number
Operator
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter .qyy?
/-/.
Probe LenijFIi and~Type_
Pi tot Tube Coefficient_
Assumed Moisture V
Sarnplo l!ov
gy: 7
Meter II /V/j
Pretest Leak Rate , c,^&
Post Test Leak Rate , (rv
I e>
Read and Record All Data Every
Minutes
Clock Time
Sampling (21-hr
time.min Clock)
O 1OO"^
/^ f c;
"Iff "k'
V< II ev
~)^t l^t
^O ~>>'f>
ic,^ 'L/CJ
IH<) 1 2 uO
}'\/} ~&>
I 6 T 9^'
i tfo 1 •? ^r^d
7 In 1o
-17.T V-T
2 5"^ ' ' /<7
? 7« 7<^
7-SS" VI"
-i'"?, V 7
f (,< 7
*/.->")
, 4. ")
^ ^7
•67
• ^"7
, /."/
/ r^> "7
* 6> ~7
fc~7
, ^ 7
,.
•^
3
3
5
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE. INC.
SAMPLING DATA .(cont.)
Hood Healer (— <^ - /
Date
Sampling Location CV«
Sample Type ^"g-
Run Number X? - /- j
Operator /4-tc /(
"N. Clock Time
Samp11ng\(24-hr
time, mlnXGlock)
^V>- ~/^«
-«,-><- • /<-
/^9<5 -ip
'/o
V9f, XiT
•Oo ^o
T^ V7
5Vrt /9 en
c,^ ' /S
%~}a ... lo
S4S VT
(pco 7^>^
<^3o ^ ii
^V^T ty^i"
d,/,rf T./ "0
£75- /C
69d ^-o
705" V4
Gas Meter
leading
(vm) ft3
?«./
•^^y.^
^/-j.c^
W7- /
VTff, <
Veloci ty
Head
UPS) In.
II ?0
r <--*/ '»,
^«V?
.c?'/S
.^V 3
* <:; V 3
- oyv
-OV5-
^^•^^r
.^^-/S
.
/.^V,
. o V ?,
.. r; H ^
. o V ^
)ri f ice Pressure
)i f ferential
(All), -in. ll?0
Desired
. c. 7
Actual
. ^ 7
- ^ -7
.<^ 7
rti
.• O'P
'0'7
*(.->
. 6 7
.-c-"7
:(n7
• G7
.(0-7
• C---7
.67
.C-.-7
,^-7
»
. 6^ ")
,.(>>-)
, C--7
• '•>?
TEMPERATURES
Di lution
Tunnel
'(eter
In
<3/
^o
p\ -7
t
£-7
TO
-
Meter
Out
9 o
9;
Hci
£/V
•;.>'o
-
-------
A-t-^f
FUEL MEASUREMENTS
Date U- ' £
Project No.__
Run No. IX - / - <-(
Wood Heater Manufacturer
Wood" Heater Model
r c_ (
Circle One: Pretest Fuel
Fuel Type- and Amount 2x4
Ideal Load Weight
Fuel Piece Length
Moisture Meter Calibration .
vJv
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f &-!'-
- S?
ES Project f A 'O
Wood Heater Model
Operators jit c /Z
f A ->
O i ^?^> C_
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
v/
H-A-1-37
-------
o
ft-l-5
HOOD IIGATEK CEUT1FICAT10N TEST
TEMPEUATUUE AMU |:UEL COIISUHPT10H DATA SHEET
ENGINEERING-SCIENCE, INC.
Client
Date ;
^-P/) Run jf A-~l-fS Test Fuel
^- ;3-^ ^ Hood Heater Model C.C-/5& Coal Ocd
ES Project 1
Time
Sampling/
Clock
fj'9i ff^-
O CJ
/ ~2C&
1 ~*f >>V
/L/(Tt)
t^ct-
(61 t>O
l~~)o*j
ff, f-c
I1&-&
"*• Cft-(,
Test
rucl
Ibs]^
i»"c,"
l<),i>
~7>£~
r1-* 1
IL .">
/?.'?)
*}»'/
tf , "5
7-
•<*L/O
'
(\ f) ;Z 3 Operators /Ji/;(' .-If!"' fi:.T
•T,.- '^ .^^t.^ — '•'
ji.S1-") IZ-S/7, C> 1r>,t, ^ o.-.l'r-'<: ,.y'
Ra. krC/ 7^-L F>r< Ilt.fi
t^l/V 'Sf/tlfffJVJlf Cl'":l/^
/C> f> fi 3» 1 //i(> - ^ "2 , 5 •*"
/02C> .-AxF Yt- / XV " i^
/Tfif '-/•6< /'f,,ej •= 7. .• ? >"£"
nty pf<,<3 y<- //•v /»»>/ A^.T yi,;\
y «; •? z v. fir /7- •>' - ^'^ ^ ^
/?v-/7/15-> O/?t"1-. PA~^~,lb?C
./' ' V
'
T— 1 • ^>
^
^ ^ 7
X 2V
•s
Cliaryc ^-' • T_> . Page / of ^
Sdrf.ice Temp.
lop
llc.ir
bottom
/I (,'•
/% ?
7./0
~i /'5
~2~Y ~L-
"2 / y
3 -'y
~3*5V
•3^9
"3 5" 5"
y IS'
light
Left
•
"
Stack
Temp .
/.•^
/ 'Z ')
1 f/&
3i"9
6^5-
Oil .
Tun .
Temp .
7i*r
""/ (i>
/\ (T
T7 /
/ <-
b 1
79
V V
^y
95
loom.
Temp .
(c~~/
^y
7?
7~~)
76
"? y
~7^-
7/
"?/
^ ^
6 9
7/
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC ISO
Date ,,-n
Sampling Location C. £?
-P-/
i^V-C/
>3^yp
Sample Type //
Ambient Temperature -~) Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
O (> S c ^-'
/? /<-
*3<3 T. p
vf" vc
<^ i? o O ^>i/
7 <7 /4~
_9<^ 3^-
/o 5" v 5"
/ 7 c» / a ov
/ 3
/<^5" VT
y ?<^ // «-•:'
/95~ /^
'Z "? T v 5"
2^ /'i.co
Zf$ /*>'
1 5(5" V?
^/"T ^5"
21-^ J?i5
7 y<~ ^S
Gas Meter
Readl ng
(Vm) ft3
jj |_ f-J/C/
5V?- S'
<77'/ *V
.
(ft'ji ~~?
<:r^<..-7
isOt >t?
637$
Velocity
Head
( PS). In.
H?0
,f~Ll 2—
,cj'/ ^~
, e.'S'-J '3
* o V?
«OV 3
. ov 3
. o^y e_
C4-/ 7_
.<>•/;<»
.-i-1-/ "i-
. t-'l :
. C7 "L-
,/V/~>
» L, 7
f t'~S
• C-'l
• Cs ^7
. f.s ^
, 6 '7
& 7
0-7
•C ~7
. ^ "7
6 "'
•47
*= -7
.c^7
.A 7
, /i, 7
4, & S
,67
ft"")
TEMPERATURES
Di lution
Tunnel
Meter
In
.S5 (- 1
<% V
p-o •:/' :
^ "L 56
7 ^ SZ
Pump
Vacuum
1 n . Hg
*7
^
'X
*"^
":^
-~z
3
Flue Draft
1n. H20
PC
I
I
to
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood lleatcr_
Date /A/T
Sampling Location - f yt7> t/
Sample Type
Hun Number '_/} ~ / -
Operator /-ii±/?
//'
• \l Clock Time
Sampl 1ng\(24-hr
time, m1n\Clock)
Ul'ZT- (£z
?7f> 1 L> it>
5
SJo 3^
$^ vr
5tfo \ 1 w
•5^C /<
o /9«<-'
/>75 /$
69* ^o
7^< V5-
Gas Meter
Rcadi ng
-7-,';. 7
•7£?. -7 .
79 V^ V
s'zs, s--
^£Et^_
Vel oci ty
Head
UPS) In.
ll?0
,0V*/
, ^'W
^ d.-1-/^
. vHG
a o v 'J
* U{/1-
* ••-( |
, 0 'i 1_
• r? V/
Orifice Pressure
Oi fferential
(All), -in'. II20
L)es i red
Actua 1
,67
•C- ~>
/ C'T
,/-..-?
/- 6- ") '
- 6 '7
«f,--)
.-& '->
• (.•> 7
^ 60
.. 6, 7
-6-;
-<•-?
- ^ "7
*<5-?
.67
, <^ 7
- C-")
> {„-}
, <, 0
• (/•?
, c, -7
TEMPERATURES
Ji lut ion
Tunnel
McLer
In
5V.
^5
S'7
s->
57
Meter
Out
ST
ST
S
I
I
4>
O
ci
-------
/V-l-5
FUEL MEASUREMENTS
Date 'j 'I 3>' 5 I Wood Heater Ma nu fa cture r
Project No. f>fr\ \VX Wood* Heater Model re / C!
Run No. &,_ \ _ -cT • ~
Circle One: Pretest Fuel - Test Fuel
Fuel Type and Amount 2x4 _ 4x4 _ 1x4
Ideal Load Weight _ _. Actual Load Weight
Fuel Piece Length _ . -
Moisture Meter Calibration MS-- _ -Sg-fr- Z. la .
Moisture Content-(Meter - Dry Basis)-Cor/-«Tc
-------
Client
Date
HOOD HEATER CERTIFICATION TEST INFORMATION
• '• Run t 4 -/~
ES Project 3
"Wood Heater Model
Operators
(==> O
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr)- , Q3 O Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidi ty (I)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (CF)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
z/ <-'
<*-i-
i f-
^,
, '-_• 1 !(. t
1
1 M£
Post Test
-L- \ • < -L- •
-7V-6S-
/•-f
v
/O rC' //fl.ft
/
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt .
Actual Coal Bed Wt.
Fuel H2CC Dry H.H
Fuel : Dry Kg /C.
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
TeT.p
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
to
Wet
\_IMJ_
H-A-1-A2
-------
A -1 -
ENGINEERING-SCIENCE, INC.
CHunt iS-V*'^-- Run I
WOOD IIEATEH CEUTIRCATlOH TEST
TEMPEUATUUE AMU I:UEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page
of
Date U-lH-'£>c/ Hood Heater Model ^T/SO Coal Ocd
ES Project If
I
I
1
OJ
Time -
Sampling/
Clock
0-70O
A"7"-/ 1
f)$\Of')
rt'V&O
(Ct&C>
1100
ri.^v
Koo
yy ft>
/V^o
//j c/Ct
l~) . Operators
•
Comments
.oioS (e.bllh 7..!°- //,i<.//,-> •.
r^ iA••.•>••, o(>J ••*
ol i V /* .3 / •* . o 5". .? *' -- '•!•(' J -
ei.'« "'
I^^C "3>$//t.^- %C'V
/V? ~L 5>t' 'r /J-ir "
f~)/'6 i/>~) /~)*<~- ~ 'l*'^'
/
f
Combust or Temp.
.^T'S
'A/.^
•(q -^ -^
Vo "i
"77ft
5 y/?
9 ^o V^o
'? f V
/^> ^>o
7T7-
9*? /
^ "5 "7
Surface Temp.
|0|)
llenr
Uottom
? 7Ci
33 c/
~^(f Cf
•376
•2.7 Co
"•% "? '7
•3 j -7 -
"Z.VT
•^9-2.
•^ 3V
2^<^
<:? i> &"
light
5^-
Left
•
Stack
Temp.
«-/oO
Si'o
•>'? -T
//'(:»
^ V^"
^ Zc'5
z,<^^'
S" ? 7
•35/-Z.
"7***£ 1
i* *7^/
^ 7 T
on.
fun.
FeinjK
t)S
*7 2.
"/'/
'/.'
7 *?
7d.
57
9 "L
^ ^~
'R'^
5^ Z.
*
•
i
i
loom.
temp .
7 7»
•7 7
/iC,'1
/, S'
7 ?
7V
69
7/
-------
SAMPLING DATA (coot.)
33
I
^*^ Uood „
ENGINEERING-SCIENCE, INC. Date _,
' Sampli
Sampl c
Run Nu
Ope rat
X. Clock Time
Sampl 1ng\(2<1-hr
time, min\Clock)
^ttn — " ' £ii
"3 V5" XC
37 £> -V>
V^>? l/^
VZ<^ /Vf'D
//'Sf /<,
^b "?
y'^'T L&'L'
1CIC> I??
4 ' lo "$&
T?
^ ?& i % 0*0
O<> /'^
(f>1 & "?«
7^*5" Vf
Gas Mater
(leadi nt)
1 IJ'L.'tf
// V ^- 9
I 111 ,. "2-
/ 2o 9/- V^
j25) in.
IlpO
n f) ijICy
.cT> V<-
fO^ *)~
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f o'y 2_
* <2 '/ 3
.o<-/V
, c- y V ^
.• n V Y
« c? V "L
o OV 3
a f l-/ ~5
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o *•/ j^-
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A (_J ~^}
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in. H?0
720
-------
TEST SERIES
A-2
RD123.40
1381A.APP
-------
Method 56 Proportionality Rate, Floo Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES/CB
1st date: 11-15-83
Run no : fl-2-1
Tst tine
(min): 600.00
Chrg ut
(Ib uet): 21.50
run
time
(•in)
0
60
120
180
240
300
360
420
480
540
600
vel dp
(mm H20)
(in.H20)
0.043
0.044
0.043
0.045
0.045
0.042
0.043
0.043
0.042
0.041
0.041
Units 1-fietric,
2=English:
Y, DGM:
Pitot co:
Gas MU :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Mood aoist (7. uet):
Burn
tunnel
temp
(C.F)
62
92
98
90
84
84
84
81
82
91
94
DGM
rdg
(m3,ft3)
313.608
344.500
375.900
407.500
439.300
471.900
503. 100
534.800
566.500
598.400
630.704
DGM
temp
(C,F)
61
75
84
87
85
86
89
88
87
90
96
Saflip vol
2 (smS.scf)
0.995 223.426
0.99
28.56 Flou rate
21.76 (dsmSm.dscfm)
0.1963 132.36
10.29
rate (dry kg/hr): 0.88
DGM dH
(MI
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/min)
965.19
1004.01
997.92
1013.52
1007.97
973.79
985.32
982.60
972.00
968.30
970.93
PR
(.7.)
106.
102.
100.
97.
101.
100.
99.
100.
103.
105.
3
3
4
8
2
1
4
0
6
4
dDGM
vol std
(*3, f t3)
22.692
22.462
22.231
22.249
22.892
21.869
22.098
22.138
22.319
22.478
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 985.60 78.50 84.36
I
t-o
I
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
PS
1
to
1
N5
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(mm):
Chrg ut
(ib uet):
run
time
(mm)
0
60
120
180
240
300
360
420
480
540
600
660
720
780
840
ORVILLE
CC150
ES/CB
11-16-89
fl-2-2
840.00
21.40
vel dp
(mm H20)
(in.H20)
0.040
0.040
0.041
0.043
0.043
0.042
0.042
0.040
0.041
0.043
0.041
0.042
0.042
0.041
0.040
Units l-metric,
2=English:
Y, OGH:
Pi tot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Wood moist C/. uet):
Burn
tunnel
temp
(C,F)
74
100
93
89
87
91
86
92
90
86
86
84
83
81
84
DGM
rdg
U3,
631.
662.
694.
726.
758.
790.
822.
854.
886.
918.
950.
982.
1014.
1045.
1077.
ft3)
426
600
500
600
800
700
500
200
200
300
200
200
100
900
571
.DGM
temp
(C,F)
73
86
94
95
94
90
88
93
97
94
93
92
88
87
86
Samp vol
2 (sm3,scf)
0.995 309.222
0.99
28.56 Flou rate
21.68 (dsman.dscfm)
0.1963 127.93
9.72
rate (dry kg/hr): 0.63
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/«in)
943. 18
965.87
971.73
991.55
989.74
981.73
977.27
958.94
969.09
988.83
965.56
975.48
974.58
961.13
951.97
PR
00
106.4
102.5
100.3
98.1
98.3
98.6
100.2
101.7
99.5
97.5
99.9
98.6
98.7
100.4
dDGM
vol std
(m3,ft3)
22.307
22.283
22.098
22. 12?
21.961
22.051
22.062
22.069
21.979
21.961
22.069
22.040
22. 132
22.082
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C.F) (C,F)
0.01 971.11 87.07 90.00
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
PC
I
>
I
NJ
I
CO
Stv *anu: ORVILLE
Model no: CC150
Lab name: ES/CB
Tst date: 11-17-89
Run no : fl-2-3
Tst time
(min): 810.00
Chrg ut
(Ib uet): 26.40
run
time
(•in)
0
60
120
180
240
300
360
120
480
540
600
660
720
780
840
vel dp
(mm H20)
(in.H20)
0.038
0.040
0.039
.0.040
0.040
0.040
0.038
0.039
0.041
0.041
0.040
0.041
0.040
0.040
0.041
Units l=metric,
2rEnglish:
Y, DGM:
Pi tot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (iti2,ft2):
Mood moist (.?. uet):
Burn
tunnel
temp
(C,F)
70
91
92
86
90
72
79
92
82
81
89
91
89
87
86
OGI1
rdg
(m3,
78.
109.
140.
172.
204.
236.
268.
299.
330.
362.
393.
425.
456.
488.
520.
ft3)
601
400
800
500
600
700
000
000
300
000
700
200
900
600
703
DGM
temp
(C,F)
73
82
96
99
97
89
69
77
85
84
83
85
90
'89
88
Samp vol
2 (sm3,scf)
0.995 308.797
0.99
28.56 Flou rate
21.66 (dsm3m,dscfm)
0.1963 125.71
15.68
rate (dry kg/hr): 0.72
DGM dH
(mo
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
0.670
0.
0.
670
(",70
vel
(m/min)
(ft/min)
916.27
958.52
947.32
954. 16
957.65
941.84
924.02
947.32
962.47
961.58
956.77
970.42
956.77
955-03
966.01
PR
(2)
104.8
100.6
99.1
99.8
96.6
98.4
105.6
100.6
98.6
100.3
100.8
99.2
99.4
100.8
dOGM
vol std
U3,ft3)
22.018
22.075
21.725
21.881
21.959
21.724
22.329
22.209
22.163
22.204
22. 104
22. 163
21. 962
22.281
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel OGM
ave temp ave temp
(C,F) (C,F)
0.01 951.74 85.13 85.73
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
ffl
I
I
.p-
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg ut
(Ib uet):
run
time
(mm)
0
60
120
180
240
300
360
420
480
543
600
660
720
ORVILLE
CC150
ES/CB
11-18-89
R-2-4
720.00
37.00
vel dp
(mm H20)
(in.H20)
0.041
0.040
0.041
0.041
0.040
0.039
0.041
0.041
0.041
0.040
0.039
0.039
0.040
units 1-metric,
2= English:
Y, DGM:
Pi tot co:
Gas MU :
Pb (mm, in. Hg):
Tunnel area (»i2,ft2):
Mood moist (7. uet):
Burn
tunnel
temp
(C,F)
76
%
99
106
115
110
85
82
89
92
91
98
95
OGM
rdg
(«,3,
521.
552.
583.
615.
646.
678.
710.
741.
773.
804.
835.
866.
897.
ft3)
305
100
500
300
900
400
100
700
100
400
400
400
958
DGI1
temp
(C,F)
72
80
89
93
96
95
87
84
83
83
84
86
87
Samp vol
2 (sm3,scF)
0.995 264.806
0.99
28.56 Flou rate
21.82 (dsraSm.dscfm)
0.1963 125.62
20.67
rate (dry kg/hr): 1.11
DGI1 dH
(itnii
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/mm)
953.61
959.32
973.85
979.93
975.57
959. 10
961.58
958.93
965.10
955.86
942.98
948.95
958.46
PR
(.7.)
101.7
102.1
101.4
101.0
99.7
97.8
98.1
99.5
99.3
99.1
101.6
101.8
dDGH
vol std
(m3,ft3)
22.219
22.320
22.234
21.934
21.747
21.924
22.175
22.156
22.126
21.914
21.874
22.186
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGH
ave temp ave temp
(C,F) (C,F)
0.01 961.02 94.92 86.08
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
33
I
I
Ln
Stv nanu: ORVILLE
Model no: CC150
Lab name: ES/CB
1st date: 11-19-89
Run no : fl-2-5
Tst time
(min): 720.00
Chrg ut
(Ib uet): 30.30
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.042
0.040
0.042
0.042
0:042
0.040
0.041
0.040
0.041
0.040
0.039
0.040
0.040
Units l=metric,
2-English:
Y, DGM:
Pi tot co:
Gas HU :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Hood moist (.'/. uet):
Burn
tunnel
temp
(C,F)
91
110
105
103
101
97
93
93
94
103
102
%
90
OGH
r
(«3,
899.
930.
961.
993.
1025.
1057.
1088.
1119.
1151.
1182.
1214.
1246.
1278.
dg
ft3)
705
100
600
300
300
100
400
600
100
500
200
300
285
DGM
temp
(C.F)
70
79
93
98
100
96
91
90
92
94
95
93
94
Samp vol
2 (s«,3,scf)
0.995 265.234
0.99
28. 5b Flou rate
21.94 (dsmSm.dscfm)
0.1963 126.30
17.95
rate (dry kg/hr): 0.94
OGH dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(m/min)
(ft/«in)
975.90
968.66
988.22
986.47
984.71
957.55
965.96
954.11
966.83
962.69
949.74
956.69
951.52
PR
00
101.3
103.1
98.8
98.6
97.1
98.3
98.0
100.6
100.2
101.0
1Q2.4
100.6
85.49
17.640
460.00
1850.00
dOGM
vol
U3,
22.
22.
22.
22.
std
ft3)
134
556
124
133
vs/VoTs vs ave tunnel DGM
ave temp ave temp
(C.F) (C,F)
0.01 966.85 98.31 91.15
21.917
21.
21.
22.
21.
22.
22.
22.
727
854
104
954
084
323
323
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Sty manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(nin):
Chrg ut
(Ib uet):
run
time
(i»in)
0
60
120
180
240
300
360
420
480
ORVILLE
CC150
ES/CB
11-20-89
fl-2-6
480.00
20.60
vel dp
Urn H20)
(in.H20)
0.038
0.038
0.044
0.043
0.044
0.043
0.044
0.045
0.045
Units l-iTi&tric,
2=Engl Lsh:
V, DGH:
Pitot co:
Gas HW :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Wood moist (.'/. uet):
Burn
tunnel
temp
(C,F)
73
10?
117
108
98
109
94
88
86
(m3
279
309
340
.372
404
436
468
500
532
DGH
rdg
,ft3)
.015
.400
.600
.100
.300
.200
.400
.400
.715
DGM
temp
(C.F)
76
84
98
102
102
101
98
92
89
Samp vol
2 (sm3,scf)
0.995 175.899
0.99
28.56 Flou rate
21.84 (dsmSm.dscfiii)
0.1963 129.05
10.81
rate (dry kg/hr): 1.04
DGH dH
(mm
(in.
0.
H20)
H20)
670
0.670
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
vel
(iii/min)
(ft/min)
915.06
943.80
1024.50
1004.86
1007.49
1005.74
1003.87
1009.70
1007.86
PR
(JO
109.1
108.9
97.2
98.8
99.6
98.2
97.2
93.3
dDGH
vol std
(«3,ft3)
21.779
22.035
21,688
22.013
21.808
22.052
22.033
22.491
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 991.43 97.78 93.56
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED
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POSTTEST B.P. Z/.-8 ^1 (IN HG)
TANK f 1 . 1 ^ ( — I.N' HG) TEMP. Z 5".
-------
r
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CLIENT .
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CLIENT J
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CLIENT
PARTICIPATE WEIGHTS SUMMARY Page L of
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ES PROJECT ft. D /2.3>
STOVE MODEL No. CC -
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-------
CLIENT
t'Pft
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PAnTICULATE WEIGHTS SUMMARY Page __o£
RUN Mo. n~ Z_- 3 Placed in Uessicator: Date/Time
STOVE MODEL No.
POSTEST
1
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WT 2
NT 3
WT 4
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DATE/TIME
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1 /. ?
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Initials
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-------
PAnTICULATE WEIGHTS SUMMARY
Page
of
CLIENT .
ES PROJECT
RUN Ho.
- 2~
Placed in Dess icatoi:: DatR/Time
STOVE MODEL No.
POSTEST
~ J
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• WT 1
WT 2
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DATE/TIME
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-------
PARTICULATE HEIGHTS SUMMARY
Pays.
_of.
CLIENT
RUN No. /)- 2.~ 5 Placed in Dessicaior: Date/Timej/_'
^O
ES PROJECT /I Q- /23 STOVE MODEL No. CC -/
POSTEST
DATE/TIME"
FRONT
FTF.TF.n II
BACK
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CALIBRATION WT.
HI MOUNT. ~
PRE WT
POST WT
ROOM CONDITIONS
RELATIVE
HUMIDITY
13AROMTRC
PRESSURE
Initials
WT 1
69/7
WT 2
WT 3
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FINAL WT
TARE WT
WT GAINED
(A)
(B)
-------
CLIENT J.,
ES PROJECT Aft /"23
PARTICULATE WEIGHTS SUMMARY Pace o£_
RUN No. n-7--6> Placed in Dessicator: Date/Time.,
STOVE MODEL No.
POSTEST
'
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
//- 2 / ($oci <$0
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CALIBRATION WT.
WT AMOUNT =
PRE WT
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POST WT
^ <$ 006
<7 5^WO
. Soo/
, 5«>0
ROOM CONDITIONS
RELATIVE
HUMIDITY
/1^^
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/ a
-------
Client
WOOD HEATER CERTIFICATION TEST INFORMATION
Run t A' - 7_ —
Date //-
ES Project i A f) /?
'Wood Heater Model CC. I
Operators Al£ $
Lu
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
L^i Xj > I">
Achieved Burn Rate (Kg/hr) 6! r1"'f Thermostat Setting
Primary Air Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (>)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
Z/.-77
f,/
i &
O
/C*- //e. <-->
Post
Test
11, -7^ •
•7 /
i 7,
^
fo.c//i;,o
I/" /
///I
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2K Dry \\ W7 Wet
Fuel: Dry Kg S.lH'
to
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Ave.
Pitot Leak Check
Static
I/
H-A-2-18
-------
WOOD IIEATEU CEUT1I:ICATION TEST
TEMPERATURE AMU FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC. /)
CHunt £fifl Run I //"
Date I/-1*5*
Hood Heater Model y£gv
ES Project. J flQ /£ "3 Operators
Test Fuel Charge
Coal Dec!
Page
of
ta
i
>
i
NJ
I
Time
Sampling/
lock
Test
:uel
«.
(Ibs)
/
Fl.ue
Draft
i'n
IpO)
.7
2*0.
2^4.
±^L
Comments
C.c/d
/; /. 9 /7, '•< - ,
9V.
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-1 x
Combust or Temp.
O/
*53o
/o -2 C-
9 0 6
S/7
T7<-
<^V6
Co'2.
V3 5'
3S7
75^
& ^r?
Surface Temp.
Top
Hear
Dot torn
<£/•
/7/
•?7f
^A^
3^6
3y?
299
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56V
Right
Left
Stack
Temp .
6/
^•99
^Vrt"?
v^g-
^9Z
Z75
ZV
-------
ENGINEERING-SCIENCE, INC.
Wood Heater CC
Date // x / ^ - ^ <
SAMPLING DATA
/I--?--
Sampling Location
Sample Type ^(^-
Run Number /} ~ 2.
Operator y/f,
Start Time
Stop Time
_
Probe Length and lype //y
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter 0 ft^y?
Pi tot Tube Coefficient
Assumed Moisture__
Sample Box Number_
Meter Box Number .
Meter H
Pretest Leak Rate
Post Test Leak Rate
G- (if
~
-3
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
C> 7/5^5
/S "^f
~2,o VT
V *) !*-/£>-&
LPO
^35 'So
/SO <-/ 5"
/65
/^c) /6-/T
/95~ ^6
7. /o •v T
Z25" <^ ^
2 VA / 1 / 5
27 1*>
2^^- r/<.,
^r>, ^/c
Gas Meter
Readi ng
(vm) ft3
~SI S.^oS
^y/«.jT
^7^, 9
-^
!
^07.5"
u^l f -\
L)~)l ^0
Velocity
Head
( PS). in.
H?0
• o lj i
a O V Y
^ o '/ 3
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* 61
,67
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^-•7
. 6 7
, ^, 7
. 6>~7
. ^' ~l
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, 6"7
•4. -7
. (,-, )
TEMPERATURES
01 lutlon
Tunnel
Meter
In
//>/
~7V
9 c)
§ 5"
S*S
•
5) ^
f", ^_
5< '7
Me t e r
Out
/, /
Cfl
7 5
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^ <^
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^> <^
Filter
6<^
•
Implnger
^ <,' •
7o
75
'/ 7
V?
7.-V V9
72 5" 7
7V ^ '?
74^ ^ V
Pump
Vacuum
In. Hg
V
V
//
C./
c/
'
y
(/
Flue Draft
1n. H20
P
I
o
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (conl.)
Vlood lleater_
Date
Sampling Location £
Sample Type *->&-
Run Number /? - 2. - /
Operator
• \C1ock Time
SampHng^x^A-hr
time, min\Clock)
"T2T5 -iSUS
-* 7< - ?c
-S«?ft VT
^^ Of
5Yo it IS
T« -^o
970 4--J-
5S^ c^
^^>o -7^yq
Gas Mater
leadi ng
(vm) ^3
sr-jy ,5?
•
'/!
x ^ V 3
^r.^i
* <• > '/ 1.
'/ •?
• r>V "Z
. o'/ 7.
.ol /
a C
I
NJ
I
l-o
-------
FUEL MEASUREMENTS
i >-= ^^'O/ .A
Date \\-Vt?~^G \ Wood Heater Manufacturer Qjol/MV.t?
Project No. ^^> \~2. ~~r-* Wood" Heater Model r_c_
Run No. ""A -~L. - I
Circle One: Pretest Fuel Test Fuel
Fuel Type and Amount 2x4 4x4 Ix4_
Ideal Load Weight ; .Actual Load Weight
Fuel Piece Length_
Moisture Meter Calibration 12% ; 22%
°F • •
Moisture Content-(Meter - Dry Basis)- CorVKTccL
Piece No. Readings Average
1 si' |AS_ ll^_ ^
2 /<-"< 3 /6.S V'S
3 i?.,<=' n.i. n.L- m
s ^' /^i k^ j^ci
6 Ii-i5. 12^-1'_i^'^ •
7
8
g /,^o ;V.6 /^_o
10 :A7 9,3
11
12
13
14
15
16
17
18
19
20
Overall Fuel Moisture Average (l.^f /
H- A,- 2-2 2
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
EPA- ' • - Run t A-2: -
ES Project }
Rfc
'Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (*)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave.. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
2/.TS
-73
"•' 'S
O
/OC./7O. O
~2/, £»>
NA-
Post
Test
2-/.
/£• .iT1
//* .
-------
ENGINEERING-SCIENCE, INC
CHunt £PA- Run I
HOOD IIEATEIl CEIITIIMCATIOII TEST
TEMPEUATUUE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page
of
_ . — . . — ... , ,
Date //—/£-<©?' Wood Heater Model C.^- <5£> Coal Oed
ES Project t
\
I
i
r-o
Time
Sampling/
Clock
ftj/LjCj
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fs^^-/ si
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i^ /,j£j
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(In
A/*J'/ "^
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,
-
Ai)/2-^) Operators
Comments
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ft,l/?-c\ ^.i.1* Q,ci^A>, /C2. <57yo
O7^C> cV tt13*"? i-ic -*> »- -v i^ '/iop*-,
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/(,T*, S^T 7,. Vx "
/
2.0 // /?„ kf<^C^/}/< /)//i TV' /-'//f
s
\
Coinbustor Temp.
•*Y 7_©
^9 ~S
i
T, <^/ •$
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Surface Temp.
lop
Hear
Uottom
~2&£-(
•
"3 ""7 "7
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"?3 ^
•52 ^
1 /" ^
V->7
277
?2 7
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2<"r- ^" '
^r, •/
Right
Left
Stack
Temp .
t*i~^
^(of
<-//&
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't*>C
1%7
2.*ao
5LS 1
'z-/t9
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1 V7
/ ^<^.'
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D11.
Tun.
Temp .
7V
A:>C
?3
39
o y
/^/ Cft
9 "2-
7^
b /
<^y
'
Room.
Temp .
~7 •?
""^ ""
7(3
7d
&C
(f "^
<• 7
£,<}
/y
•73
•J&
6- ?
(a
-------
ENGINEERING-SCIENCE, INC.
Wood Heater___CC-/5_^
Date
SAMPLING DATA
/;- /6 -
Sampling Location
Sample Type
Run Number /V_
Operator
Start Time
Stop Time
Ambient Temperature -7^
Barometric Pressure -2.A '75
Static Pressure, (Ps)
Filter Number(s)_^
Meter
Q, 9
Probe Length and Type_
Pi tot Tube Coefficient
Assumed Moisture •
Sample Box Number~ /-)
Meter Box Number =
Meter H
/£//;
A
Pretest Leak Rate .003
_
Post Test Leak Rate•„,?,:<•/ (aJ fo
Read and Record All Data Every /,, 0 Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
n fY-* t-i c:
/5
3o
Y5
c,o 67 V^
75
10
fC.C,
f^e,
750
/6S
£BQ 0 9
Z/o
Z (t>*-c5
-55
T-,^
^2?\5
TOO ^YS
^^
•?Pto
Svs
36,0 ^ZV5
Gas Meter
Reading
(vm) ft3
(^ ?. t»
<-fc/l
iPV /
. <>*/ 1
.<:'V3
, °Y 2-
.fly ^
/'j *-/ 7
.(if -^
,di /
.6 ~7
.6. -7
v<^> -7
&~i
• (3—?
lC*~)
' (' "1
, t., ->
, t, -7
ic "/
• <^ "7
, C 7
^ 6 '?
,6 ~i
C~7
.6,7
,6.7
TEMPERATURES
Oi lution
Tunnel
Meter
In
—p«y
<9^
9^
9<^
•9-2.
*7o
9o
Meter
Out
"7 ~s
f>S^
f?V
95
i
ro
I
NJ
-------
[Bsnaifjpia
^j^ra tiuE~v
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood lleater_
Date //- /
Sampling Location_
Sample Typc_
Run Mumbor
Operator i-i-
*
\^ Clock Time
Sampl1ng\(24-hr
time, min^\Clock)
37xrt /JLZS:
-?-?c • <-*>
-^9o /?
V^^T 5o
LJIo /3V^
V35
V5'0
^65"
v.^o /«vvs"
y?^
s-^d
57-S
5-/<9 /s'-/\-
i'C73
ST-J
585
^0 //. cyc;
/&' 5
(,30
foV^
{.rno n^S
feU
6><1i)
16*
Gas Meter
Readi nq
(vm) ft3
^•5'/ Z.
C8C 2_
9 / S' - -3
9£o, 2.
9^^,?^
Velocity
Head
(APS) in.
IlpO
rl>V I
^o^ (
,dVO
^ O'X^
. & ^^
, o-/C
.o-l I
. o<77
o
,l'7
.47
-67
t. /^ 7
, ^7
o 7
.r-7
. A 7
. ^ -7
TEMPERATURES
Di ution
Tunnel
'leter
In
^4-
?:^
«jr-5
_9J_
97^
Me t e r
Out
97
77
9V
•9'^
^^
Filter
3/
53
79
•7 7
77
Impinger
-5- s
f^'o'
-------
T/pssa
&23TJ
•S-stFI
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
V/ood Heater
Date //- /c
Sampling Location_
Sample Type
Run Number_j
Operator /-/i
C ~ / ^ Cj
• ^^ Clock Time
Sampl1ng\(24-hr
time, min'vClock)
-)o~Z -t**2L
-720 /3VS
->?<; **
-)^o sf
-)&.<$ -3o
-71J-0 !*!
WJ 2»
-------
A-
FUEL MEASUREMENTS
Date
/ Hood Heater Manufacturer OfJ,l(s>
Project No. £ L> / 2- =*
Run No. /A^1 — —* -
Circle One: Prete
Fuel Type and Amount
Ideal Load Weight
Fuel Piece Length
Moisture Meter Calibration
st Fuel
2x4
*
J3Z
Wood" Heater Model ex. /s ^
(fe^_FueJU^
4x4 1x4
.Actual Load Weight
.
• -£2T^ d"3
/
TV /»! a, °F
Moisture Content-(Meter - Dry Basis)- Co»vK7tci.
Piece No. Readings Average
1
2
11
12
13
14
15
16
17
18
19
20
Overall .Fuel Moisture Average
H-A-2-28
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run j
ES Project i
"Wood Heater Model
Operators ^>J j
CC/STp
, v\ K<- {\
TEST RUN INFORMATION
Attempted Burn Rate1 (Kg/hr)
Secondary Air Setting
Ach.ieved Burn Rate (Kg/hr) Q..'~'1\ Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume. (ft-)
Fuel Charge Range Wt.
Pretest
•2./.S"?
(j-i
1*1
O
16-0/10 O
AJA
Post Test
1. f . 7 '-f-
f,-,~)
/<%•
C>
1C . C' //(.- i.<
f
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt. _ _
Actual Coal Bed Wt.
Fuel H20% Dry Ar.Gi Wet
Fuel: Dry Kg /•-'. CT
to
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Velocity Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
H-A-2-29
-------
A- *--
WOOD IIEATEK CERTIFICATION TEST
TEMPEHATUIU: ANO FUEL CONSUMPTION DATA SHEET
E.NGINEERING^SCIENCE, INC.
! Cllunt pP/7Run II
ES Project /f
X\-2.-
Test Fuel Charge
. Page
L
Wood Heater Model CX" /5° Coal Bed
Operators £,-
Time
Sampling/
Clock
Test
Fuel
•/t.
Ibs)
OS 3o
to
/J3.Q
3.3
, 7
l,ue
Draft
(1'n
o.Qiy
63
Comments
iiA<
. S
y /
A, ft
Coinbustor Temp.
frvy
5V
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
Sampling Location
Sample Type ^
Run Number /I,
Operator
Start Time
Stop Time
00 "3^.
Probe Length and Type . /y
Pi tot Tube Coefficient ._i
Assumed Moisture t-f
Ambient Temperature
Barometric Pressure
Static Pressure, (PjT
Filter Number(s) "
Meter o
Sample Box Number^ /-}
Meter Box
Meter
II
2A:
Pretest Leak Rate L>,
Post Test Leak Ra.te ^^
lj
Read and Record All Data Every &O Minutes
Clock Time
Sampling (24-hr
time.min Clock)
0 0(^0
(3
?£•
V?
£& tX7^0
7^'
CIO
lo1^
/?-> £>'3'?>'^
/35"
fM ^\
lt\o ocv"3o
(9 5
~> to
7 2*5
-) t/u ;o 7> t>
"^
770
2(95
l^o / / ^ c^
^/^
llf-y
"V/5
T-O / ? 1>O
Gas Meter
Readi ng_
(V^,) ft3
/o^/i y
i^i^.^d
,
/77-. ^"
"Z-^'V, ^j
7 J 0 , 7
7 6<^,O
Velocity
Head
( Ps), in.
H20
ft, o 7> &
6,Cj^CP
t>,cw o
(^, 0,-^t^
6.o<-/ "
(>&3 °/
O.o'^>7
J/C'S^
d>, d^Cl/
(Di^'S'/
^.D^/O
6,^V^>
a /> V,:.
,(3V 0
-, r, V c,
.OVO
, C '/O
oyci
<3*yc->
.(, •/ ^
„ «VO
. o Vo
..o ^ -^
Ori fice Pressure
Differential
( H), in. H?0
Desi red
-(j>""7
Actual
• if"\
,d>~~~f
.(i) ~~1
.(j ~~>
i C ~)
.<-,- 7
'(-'"7
-(» 7
, ^.-- ~>
•'"7
/ c--?
6 "7
, 6-7
,47
.6-7
•CO
• (• '?
.67
^ 7
<', ~7
^. ~>
.6 -7
. ^ 7
^^ -7
TEMPERATURES
Di lution
Tunnel
Meter
In
"7 "*,
SJ
^ ~>
9cp
°l^
fi 7
3'J
6- 9
Filter
f-£
•
Impinger
(••> 7 '
t^o ^ <-/ •
B^ <# /
^'o ^ 9
I
N>
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood Heater ( f - /
o
Date //- / 7 - 5 1
Sampling Location C ,
Sample Type_
Uun Number^
Operator X-JL
-1
>^L
is
\s^ Clock Time
Sampl1ng\(24-hr
time, min\Clock)
'Tff2 : 03°.
1 7T • #f
1>clo v<>
Vot i*
Q10 /V4<>
'VI f V^
V5VJ oo
Vtf IS
V«^> /"y-V>
*/9«? «yi
-5/n ^?^'
?Z< / 5
f»"Vo /S^o"
^C< ^
57o oo
5^ /^
L> oc? V 6 3O
^V<" IS
(P^o n-^o
^75 V^
£,9o ^^
-7o< /9
Gas Hater
Reach nq
l^n.) f^3
•2.79^
? ^^, 3
~?^2 , C
•^ftjr)
vis. z.
Veloci ty
Mead
(6PS) in.
ll?0
^>,63M
« r> V.<
.0 \-4
o V^Cl
a 0<-/o
~OV()
o^V/
d, O^/
^ t>'Yf>
*«v /
* r/v/
, 0 V/
» r- V/
v ^.' f 0
. oVo
/i O '/ 0
,0^0
• a'J*
* c- V r,
» o V/
- o Vo
j r; V 0
. C-'/O
Ori f ice
Oi f ferent
(All ,-in.
Ues red
ressure
ial
_MZ0
Actual
>~?
«^1
* <>7
. 6, "7
t^-?
*(.-)
,6~->
a & -7
-07
. 6 7
.67
,^-;
'/- 7
' -t.-)
- 67
r <• 7
, ^7
r Co 7
- 6-7
,t,~)
< C' 7
, c>7
x 6 7
TEMPERATURES
Di luLiori
Tunnel
Meter
In
%/
<*$
«v
•S-3
«6
Muter
Out
77
*s-
•K/
V ^
^S
•Miter
-7 V
^
73
7
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
CC -/5o
Wood Healer
I/ -
Sampl i n? ' — — — <£-i^!5L
720 /tf'^J
^^•> '/^
9^0 "0
76* >$
-7«0 /^-3fi
>^ V5
p C'<-/C)
, r?V<7
,,oV/
.r?V^
„ oW
« c? VZ.
^ o'v/
a ft <-/ /
On f ice Pressure
)i f ferential
(AH), -in. H?0
Desi red
Actual
.- {, 7
.. /-,")
.-G~7
*
* ^~?
•&-I
'C~>
*c n
e& ~?
TEMPERATURES
Dilution
Tunnel
Meter
In
9o •
^?
&rk
*-?
-
Me t e r
Out
9^
3f;
ft-*
.
Filter
7*'
7£
->(,
"
Impinger
5')
<;%.
<;x
•
Pump
Vacuum
1n. Hg.
^
^
<;
Flue Draft
in. H?0
• I
• i
I
to
I
-------
FUEL MEASUREMENTS
Date ll-l"?"''^ ( ' Hood Heater Manufacturer C. Col('\
Project No. I' C> t "2, ~"S Woocf Heater Model r-c / s • 6
3 /C_& /C.5 ^-3
4 /cH__ //.5 f/ilf.
s ^o° -?_i.^££ 2iS
6 ^S'J_%LL ^L~
7 . //V '^T //,2,
9
10 "c.e "LZ.y
12
13
14
15
16
17
18
19
20
Overall .Fuel Moisture Average
-------
Client
Date ii- rg. -e
-------
HOOD IIEATEIl CEIITIF1CATIOH TEST
TEHPEHATUUE AND FUEL CONSUHPT10H DATA SHEET
ENGINEERING-SCIENCE, INC. / ,
Client Zf PA Run I AY-?-'"/
Date /;- /g - 2 7 Wood Heater -Model Roo
0^700
A' C&
\\£>o
12 trO
/?£T-J
IV c-cj
IB crt)
l(}^t>
/~) i-n
/« <3^0
^/3^
Test
Fuel
Ht.
(Ibs)
3>'l
/2. |
~)r~*t
~\ c<
"•7/5
2 ^V
^ » f •»
2*5
/// o
^/ ' Y
•^ , ••)
7,-i
Fl,ue
Draft
(in
iiGZ-1.
.O^/ GI
aif/Cp
O^f-)
i &(-«*>
»o5"9
• b '%•>
t <^yy
•i!"?/l
• PVti
n£>^ 1
f^V?
.'-3/l,/ 2.2-^ K'*l!'-^ c« /(•'.-./
r-^^? >i."^ r^1 •/ '
f-f.^/'^C1 n.o^ ^c^c-.:C a c.f \vi
C(,3/^,'2_ 7,( f^arK, (^ //^/7
/3 <^
/'lo^ ^3/7- //& ^v ''
<^,'i ^ A>iS «ij \T w-> y ""
/<-^^c7 /?//« Vo <**1 4 •>
-
!<•
Combu
3c
-7
?/
<_~^
^ 3
^
5
5
5-
5
So
7
*j
Test Fuel Charge
. Page / of S
Coinbustor Temp.
3 <;.-?_
-7 2 «
?/ Y
9?^,,
/3 /6
^T
5 ?/ .
529
6"ov
?^->
/i /r/
7<^o
-J7-7
*
Surface Temp,
lop
Hear
Bottom
?2'>
T45/
^^^
<-tl-J
-/3'7
•s y?
•*£/
3 2y
^/Y
~*>o-o
•2, -57
•^-7 ?'
3tfi^
Hi gilt
Left
Stack
Temp .
-v-7
VrO
•0^
5"//
(".
u*i
I/O
&S
S7.
K9
<)?.
'V
9"*
9r
Room.
Temp.
77-
ciV
^ 1
fc~7
^-9
76
/,y
6 y
<;•?
t,-i
^-^
^-^
6 7
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
. -
Sampling Location
Sample Type \\
Run Number
Operator
Start Time
Stop Time
-,'s-V-C:>
Probe Length and Type •
A - -
Pitot Tube Coefficient
Assumed Moisture
Ambient Temperature
Barometric Pressure
Static Pressure, (Pj
Filter Number(s)
Meter C
Sample Uox Number/)
Meter Box NuinberAL£-f/! f-\
Meter H
Read and Record All Data Every
Pretest Leak Rate
Post Test Leak
Minutes
Jotff
Clock Time
Sampling (24-hr
time.min Clock)
£> /,£>Oci'>
l*>
7o
(fO O^OO
7^
9 /(oo
/•^S
2^o
2ZS
> i^c,
Z70
?K^>
^(•c-,
33^
IkP i L(PO
Gas Meter
Reading,
(Vn) ft3
55" 2, 1
£~ & ^ x*
^J D ^ j \7
,
///;, ^
^•y^.. <9
67^? y/
7/,o. /
Velocity
Head
HjO*
fi.04 (
£\ C'VCJ
6i^VO
/> (OVO
d. ^ L,- /
j/) *OC/O
• (.>"-('
.oY/
• L t:^/ 2^
<:>-/ /
, O<-/ |
• ' i
.&<•/!
a 0<-f<>
^7-59
^, C7 39-
„ c> •? 9
^ ")
(f"7
. l, 7
-07
• 47
/6 /
, /., "7
,£ 7
i(f~)
./J."7
.6*7
• ^ 7
-/-"?
TEMPERATURES
Di lution
Tunnel
Meter
In
It/
f' ~*>
9 /
•75
r/5
<9 ^
sr^
Meter
Out
"7 Z
?•:<:>
S r;
V"?
^"^ C'"
dj ^~"
f>
97 • ^/
7V
to
Pump
Vacuum
in. Hg
<-/
H
I
N>
I
U)
-------
ppui jrjsrj}
K-Sra tXttZSh
t-rt-rrrr/}
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater C C ' /
Date // -> /
_s_2_
Sampling Location
Sample Typo
Run Number
Operator #.*
"Z-
2 -
• \ Clock Time
Sampl1ng\(24-hr
time, min\£lock)
37JTJ — • • — -—ihLaSi
17T -if
t/uC; Y
V"?*r~ ^ *r
l*5~O ~*tt>
V/-T Vf
^2# /„£> <-o
y?y /<;•
*)/& ?0
57^ VCO
/0/5 }*?
&3& 36
^y5" y?
6<^^ /?^<>
£75" //^-
^9^ 3<5
7o^" V^"
Gas Mster
Readi ng
7//. 7
•77-%. /
^^y, y
sj -^ ^,y
H 1
*0ci
ft & ""? *v^
., f.> VO
f f ~l c/
*o ^>ci
f o 3 r\
0 dVff
*ofo
Ori f ice Pressure
Di f ferential
(All), -in.
Desi red
m
1120
Actual
.£.-1
»(.-, '?
' 67
- 67
„ ^ 7
I(T~)
,(,^)
,67
. £ 7
* 67
. «r. 7
* 6 7
,
-------
FUEL MEASUREMENTS
Date (\'i&-'&0I Wood Heater Manufacturer
Project No. fr ft f 7. IL HoocT Heater Model PC i SO
Run No. AT- ? ---<-/ '
Circle One: Pretest Fuel • . Test Fuel
Fuel Type and Amount 2x4 _ 4x4 1x4
Ideal Load Weight__ _ .Actual Load Weight
Fuel Piece Length _ . _
Moisture Meter Calibration 125 _ 22? Z,l>, [
\J«*d r»/na. °F _ • .
Moisture Content-(Meter - Dry Basis)- Cof/'KTtcL
Piece No. Readings Average
1 $•' ft6_Zc?*_ ?*_^
2 Z7v3_Z^2. _iL?''G
5 d'£"
6
7 tf^_ /75
s 7r" 33_^ ra;
9 /k,/3_ O9
. -n
10
11
12
13
14
15
IS
17
13
19
20
Overall .Fuel Moisture Average
H-A-2-39
-------
Client
Date
WCwD HEATER CERTIFICATION TEST INFORMATION
1 Run t '
ES Project i
t
-------
5
WOOD IIEATEU CERTIFICATION TL:ST
TEMPERATURE AND I:UEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Cllunt /?£>/£ Run II
s
Test Fuel Charge
( .r
Date //-/*}-£> 7 Wood Heater Model L.C f~>CJ>
ES Project 1
sc
i
i
NJ
1
1 — •
Time
Sampling/
Clock
OlHOQ
Ci^i O O
1 £o£_->
//
lfa cm
l~J ert>
/% *rt>
/7
/« '\
S,S
5.2-
"i--v
o c/
' * V
6> • 1
"*>*(/
~2 * ")
•2 .-2_
Fl.ue
Draft
(in
O.fi1/ S
,6-V?
6,c.C»'fo
/
* <9 "^^
r>/^ y/
«£>£->
e<3V7
nS/fL
tri'Vl
'
/^fV?, "\ Operators io/iH \r{'$\
.
Comments
.^«rv,r oiwj" ' ct* f fXaiv:
ll.S //•?» XJ '•"l-S-11 ti--'';V' >('('-> Cp- IS
/Z.7/J..3 /I.t/tfc-^4'c^e-iz^f5
It J 1 ^,>- seV Ci -v Ki of-
,
(5/3 /2.//3.^> ^I
^^^
-?c>6,
v;<37
^/^^
Surface Temp.
lop
Hear
bottom
Z7f.
35 /•
3->/
Vo'l
15&
^<7
Tx^/
3^^
33y
^xz^"
'7
3V <-
Right
Left
Stack
Temp .
VSf*
^r-9
y/7
^7^
Z7C
-3/5"
3?S
?o
f^
6f
7V
~7/
-?/
49
^<5'
7/
-^^,
^v
•?/>
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
A-
Wood Heater
Date ' < //-/•?
Sampling Location
Sample Type
Run Number^
Operator
Start Time
Stop Time
Ambient Temperature
Barometric Pressure
Static Pressure, (PjT
Filter Number(s) "
Meter *-_ , yy*
A Mr
Probe Length and type (<-i '
Pitot Tube Coefficient , *? "7
Assumed Moisture t^&
Sample Box Number_
Meter Box Number
Meter
II
7$:
Pretest Leak Rate ^
Post Test Leak Ratepf^z, Co &) /o
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
time.min Clock)
t-} &/\oo
/*>
t/^
/j &c\£"->
75
/6S
720 (f^O^
/5'6
/65
/ ^c) / ( & ^
G^T
2./O
72"^
Z V<^ / 1.^1^
Gas Meter
Readl ng
(vm) ft3
^/v. 70^-
<736. /
C^ 2 l/ ^7—
6^/. ^
.
<^~ii3-"3) ,
-
> o2.£j. *,
2.5'S
770 .
-j^-i — _ i
<4CX-^1 /^cJcS1 1 O-S7./
— . , 1
Vel oci ty
Head
( PS), ^.
H20
6-C>c/ ^/c*
oy d
, 6^/^
, £*7'O
,. OV-"<
, o V 2-
. 0 V
.o<^X6
, o «-/<->
. o *-v /
Ori fice f
Differ*
( H), in
Desi red
'ressure
mtial
. H?0
Actual
^ ~7
.(„ -7
•
96
Filter
Implnger
(^V <^£/
<95 fT7
<9 ^ "5 c
^y c^-c
5j <^ <^ ^
S^-> "C'"5
Pump
Vacuum
1n. Hg
-^
^z,
7)
3
•^
^-_j
Flue Draft
1n. H20
.
-------
{\-z-s
35
I
I
-P-
OJ
KLgujj x.fy,?nx SA
ENGINEERING-SCIENCE, INC.
•1PLING DATA (cont.)
Wood Heater C.C /SO
Date
^-/9-??c/
Sampling Location C /-^
Sample Type
fScr/
Run Number /\- -2 - -5
Operator f.,\MM , J Me K '
"\. Clock Time
time, min\T.lock)
• ~
*"b73 '-//vi
•39 o
l/Oe;>
1Z& 1 5^'Q
y*)*? / 5"
V ^ <9 ~*>&
^/^.'7 V^T
V5£> /<£ ^^
^/ 9 'T /"9
£/# "3^>
47f v^
fVo /7t&
^S^ / ^
<^~PC> -7<3
c?<" ^5"
/^ ^^>
/ (it? V4?
<^.66 / 'ni' . .
//y 9" < 6>
//$/. 1
// SZ-"?"
'Zyy, 2,
/• :? t,/ "2
Veloci ty
Head
(APS) in.
ll?0
O^*1-/ /
,oV i-
.OV(J
,,0 VP
x\ t_y ^i
i\t-'/ ()
i^V/
„ c»'y/
<^V --
.o1-//
no y i
. n ^o
o^/ /
. t7 ^/
* <3 3*7
.^J^
. o 39
j. /^ *-/ S>
a O Vc»
, o y^
«c) V" ^>
y <° V
Ori f ice Pressure1
Oi fferential
(fill), -in. H?0
Desi red
i Cf'~l
Actual
. is>'~l
, 67
* 6 "7
<(f>~7
• ^ "7
^'~7
-<^ "7
• -7
67
,
TEMPERATURES
Di lution
Tunnel
Meter
In
9/
<9 z
<0}C/
c/6>
9 *5
-
Meter
Out
9<9
^ -7
^ ^/
<5 T
*? 3
Kilter
SV3
9y
£ "7
<5 S
^/
Impinger
*> 5"
$ H
^ £
^ 8
•
SC
Pump
Vacuum
in. Hg
3
^
^>
"~"
~*,
3
Flue Draft
in. H?0
53
-------
FUEL MEASUREMENTS
f**>cy (^ • * 11
Date I \ - I 1 -" O I Wood Heater Manufacturer UlO*X\.\;
Project No. P ^\ i ? "X
Run No. A-- ~> -^
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
Fuel Piece Length
Moisture Meter Calibration 12%
Wood" Heater Model CC, ( *
^
(5jst Fuel
4x4 1x4
.Actual Load Weight
22%
^ Q^
^3 /
TV /»=>.
Moisture Content-(Meter - Dry Basis)—1
Piece No. Readings Average
i '^ / (3.0
3 I3.3_ {-:
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
13PA- • " Run , 'A - Z -
-------
A-Z-C.
HOOD IIEATEH CERTIFICATION TEST
TEMPEUATUIIE AMU I:UEL COIISUMPT1011 DATA SHEET
ENGINEERING-SCIENCE, INC.
Cllunt ____EP/L_ Run
Date
E5 Project t
Hood Heater Model CH: P
Page
of
ine
ampling/
Clock
1 1
\1.HC>
Test
uel
.
Ibs)
F.ue
Draft
(In
a<-n
Comments
-7
Couibustor Temp.
!^oo
/^7<-
Tc>5"
/ 2^-^
-7 ZT-
C/1V
S'OV
V9/
V^-T,
Surface Temp.
lop
Hear
Uottom
-2-/ 7^
'3V 17
•y^o
<-)Z^^
ll'ti
317
27T
7.^*9
Kiglit
left
•
Stack
Temp ,
)5f
VVZ
5B3
<;.??
v//
^^v
27?
27
-------
fpa&
i 12
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
Sampling Location_
Sample Type
Run Number A -
Operate r .
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter Y -
Start Time
Stop Time
C>
Probe Length and type
Pi tot Tube Coefficient^
Assumed Moisture •<
•Sample Box Number
Muter Box Number /-
Meter H
Pretest Leak Rate j,
Post Test Leak Rate r->
/5
-7^
7o
Y5
co aSv-s
75
7-5
/ "2
V6S.V
Velocity
Head
( Ps). In.
H20
O.G^fi
0,0^ A
,r>3 "P.
,c>-^^
.<>3(A
X^L/ "?
, dvy
. oy 2_
- 6 V 3
j. ^ W
» W
Orifice 1
Differe
( H). 1n
Desired
.6/7
.67
ressure
ntial
H?0
Actual
>Co~7
•C "7
.C.-7
.«-„ -7
. (o "^7
• &> 7
, ^ -7
• (*>-/
. ~>
TEMPERATURES
Di lution
Tunnel
Meter
in
77
f\~f
79
/(. 'Z-
/£•/
lo~t-
V7
Meter
Out
-76,
£•'<•/
"i'r\
J{- "L
/ f> 2.
/o I
^%
Filter
1 (
•
Implnger
&(t- fr<5"
*"/ "S S" ^
9o 5" 5'
^5 "7- ^9
Cf & 6>t-
.y ** s • f
Pump
Vacuum
1n. Hg
-^
^
•~\
-?
-5
1
'^
Flue Draft
1n. H20
I
>
I
N>
I
4>
—I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater C C- )
Date //- £o- &*?
Sampling Location C
Sample Typo 5"c/
//
\. Clock Time
SampHng\424-hr
time, min^^Clock)
TGB — o
3"7o 1$
V«f 3d
Vzo /VV5"
V?5 &i->
LJ^O J5
^^ 1"
V$a /5V^
Gas Meter
Readi nq
(vm) ft3
5bt? . V
5-?Z, 7/5"
Velocity
Head
(APS) in.
"?°
• ^VV
,0
<
*6> -}
>{- ~?
TEMPERATURES
Di lution
Tunnel
Meter
In
°H
^0
-
Me t e r
Out
:11ter
»/
•X&
Inipinger
^C
<:^
•
'ump
Vacuum
in. Hg
"1
3
Flue Draft
in. H20
1
NJ
I
-------
FUEL MEASUREMENTS
Date //'7-S -g"^ _ Hood Heater Ha nu fa cture r
Project No. ^>D I 2, "x> Hooo" Heater Model QC /'' S;| «' ^
Fuel Type and Amount 2x4 _ 4x4 _ 1x4
Ideal Load Weight_ _ .Actual Load Weight _ ___
Fuel Piece Length _ . _ _^
Moisture Meter Calibration 125 _ ' _ 225 ___ ~Z-~3>
u/«c<^ r* -, s. °F _ _ • ~ : ' ~ - :
Moisture Content-(Meter - Dry Basis)- CorvscTcci
Piece No. Readings Average
2 U.Z. H.3
_4 '-v_f ""?-3
s 75^ ^."-r q.7
6 //£_ (41.
7 /.XC //}P,
8 ll£J_ ^-5
9 7V<" 'M/ ^7
10 5-r/ /C'^
11
12 .
13
14 .
15
16
17
18 .,
19
20
Overall .Fuel Moisture Average
H-A-2-49
-------
TEST SERIES
A-3
-------
TEST
A-3-1
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
33
I
Stv oanu: ORVILLE
Model no: CC-150
Lab name: ES/CB
1st date: 11-28-89
Run no : fl-3-1
1st time
(«in): 619.00
Chrg ut
(Ib uet): 20,40
run
time
(mm)
0
60
120
180
240
300
360
120
480
540
600
649
vel dp
(mm H20)
(in.H20)
0.048
0.047
0.048
0.048
0.048
0.047
0.048
0.047
0.048
0.047
0.047
0.048
Units l=
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED
// - 2 <6 ~^ *7
DATE RETRIEVED //-•? 5 - 8 ^
-
WEIGHT GAINS
PROBE
LINE
CONDENSATE
1.7
•-,
* /
TEST TIME
TEST LOCATION 'C/V$j£t/ f}-*7T< FILTER* 1 £ S, '3 STOVE ID CC-/CO
SAMPLER SN# FILTERS Q WOOD SPECIES/^,«-c.//y A/,
WOOD MOISTURE (Z DRY) 2/,
7 —~
— WOOD MOISTURE (7. WET)
TOTAL (MG) /
(HG BAROMETER UNCORRECTED)
PRETEST B.P Z.|.-"7 (IN HG)
TANK 7-1.35 (—IN HG) TEMP. JO (C)
TORR ABSOLUTE
POSTTEST B.P.
*7)
TANK
( — !>; HG) TEMP. Z.O (C)
TORR ABSOLUTE 1," '] , ? i'
PRETEST LEAK CHECK
HOOD CONSUMED (LB) jC'.^l (KG)]
SAMPLE FLOW RATE PRETEST
ROT3SETER_
POSTTEST
ROTAMETER
(ML HIM)
START
(IN aao) FINAL J;, "3 (IN H20) LEAK RATE
CN H20 MIN)
POSTTEST LEAK CHECK
START S.C? (IN H20) FINAL $ 5 (IN H2) LEAK RATE ^- ^ (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(%)_
CO(Z)_
02(Z)
RUN COMMENTS:
'. V
& lit- PROBS^gagBS. 7.7o29
erwric LIME •
MIN.
7. 2C/V.
---^r^^
ITROGEN FOR INDICATED TIME
+ MIN. + MIN.
DELTA
.. — •
-------
CLIENT
ES PROJECT /?/)
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No.^l7~/9 ~ 3 "/Placed in Dessicator: Date/Tiine^ll^
STOVE MODEL Mo.C
-------
CLIENT
ES PROJECT
SPA.
PARTICULATE WEIGHTS SUMMARY P
HUN tio.Ufif-/? 3 (. Placed in Dessicator: Date/Timo^i^
STOVE MODEL Ho. CC ~ / "5^
POSTEST
Acetone Lot
Acetone Sample Volume
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
i~L-/(y/iy
//~^39
HEAKRR II
/)- 1
^0 , (-C Z,
POST WT
*)& . f?'C Z.
*>OfC'Csc' {
/
ROOM CONDITIONS
RELATIVE
HUMIDITY
I^C,-*
ct Q$ &
BAROMTRC
PRESSURE
z/'tr
-i/, ^
Initials
/^<-/?
ricft^
(BLANK CONG.)
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICULATE CATCH (A-i-B+C) =.
-------
P ARTICULATE WEIGHTS SUMMARY
Page.
_of.
CLIENT
RUN Mo.
^
Placed in Dessicator: Date/Time../
••?*?
ES PROJECT /? 0 " /2 "V STOVE HODEL Mo. C.'C ~/^j
POSTEST
Acetone Lot II
Acetone Sample Volume
'.
. WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
n
TARE WT
NET
DATE/TIME
I2~ > @/*y$
l-L-l&ll/o
H-V-'b0!
BEAKER II
A~ ^o
79. 5V$6
~?<}t ryzY
-7°!* ^VW
•79.539^
90&^C\
'CALIBRATION WT
WT AMOUNT -
PRli WT
$0 . i'C.'TJ /
*Tt1 . f>e-nL, "l_
POST ' WT
So.tiTe'i.
^O.CfC'O /
ROOM CONDITIONS
RELATIVE
HUMIDITY
/S<%7
/^^y
-
BAROMTRC
PRESSURE
Z/- V
X/,^
Initials
/£i<^
/llc/{
ta
i
>
i
OJ
I
»—•
i
Ui
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
* c;«- S y
(C)
TOTAL PARTICULATE CATCH (A-i-B+C) =
,„,?.
-------
Page / of
CLIENT J
ES PROJECT ft P /2 3
PARTICIPATE WEIGHTS SUMMARY
RUM No. /) ' ~$ - I Placed in Dessicator: Date /Time
STOVE MODEL No.
POSTEST
1 WT 1
WT 2
NT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
(I-/ &/*/<
1-L- > ($>/$/#
H-2& 'If I ^
//- l^c/
FRONT
FTLTRR II
A£-ltf
l.Hl&S
/*V3?y
/-vszy
l*1<$<*5
* 6*6/7
.^oY^
BACK
PTf.TKR II
A£-fcC
5iV
CALIURATIOH WT.
WT AMOUNT =
PRE WT
«^«y
.- ^OL-fS
« *)•&*'•&
POST WT
, 6"<:'£V^
/y<7?7
^ *yt>CTs
ROOM CONDITIONS
RELATIVE
HUMIDITY
/•*^67
/9^8'
/tf<&6*j
BAROMTRC
PRESSURE
t/.'*'
Z/- S'
Initials
i
/*CX
/*<
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client /T/0/» Run / /?-?-/
10 //
Date //- 7. % • 5*7 ~"~ Wood Heater Model
ES Project t R 0 /2. 3 Operators /fr 3
/ Fuel H2« Dry I /, 3 Wet /?,
Fuel: Dry Kg ~7^ X-
^ LOADING/TEST START OPERATIONS
7~ By-pass a.r ^~-
-------
WOOD IIEATEIl CERTIFICATION TEST
TEMPEUATUIIE AIID FUEL COHSUMPTIOII DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £~ />/?Run f // -
ft /
Test Fuel Charge fo.3 /c
. 1°
?c
3 Z./C
J
TySt?
3 •> 6 cr
Time
Sampling/
Clock
1 0 7 o
16 "ZT-
/'o<-/O
//
// /
12,15
11 1 f\
i 1 ?> 0
1 "*i *>O
/<-< 3 0
/// "if
/? ^A
i S s~?
Kl-rA^y5"'
•2-0 -^5 n
Test
:uel
n.
Ibs)
(3 1 o
•^/l_
/.
Fl.ue
Draft
(in
«i'O5i>
*'«i^"J
.f6f
* !?V Operators/JK^ <^ J /-/
' Comments
.T/r CT/. rrA,
rll«^f /^ /? lM,.If,« \nTltf C,C* i>-
K/n-dl.n'f, a.i-?i\i
I\,^(
, „ ; 7^. 1 "i \
3 i ' ' ^
C. L~ -ie ^ ftm) Cto T* ^ t>s rs> «" :•
d^t'^' ff7 7/> / £•
// P e-k, D . 1 Xf7 /&/« •*..
(y ,n euT / o.n/^,1 % /' , / oAfe
7;
Combustor Temp.
r> z.
5" c /» /v
/
fa ~L i
V * /
6~? t
775
*79 5
/C' "Z 9
r^ 2_
"7 / '»''
VV<-
S"o6
T"?7 "
V^" ?
c?
"2 / 6
27-5
3V3
3 ?o
? y V S'
V6 2
•9 <^ "i-
S'Jy
V6'/
V^'Z-
2»7
"?>"/
53V
"Z ^3
J2-^i-J-
"i"7 ">
^^r
'2~>S'
"2,
on.
Tun.
Temp .
*} 3
III
/ Z
S ~5
K '?
TV
"77-
">9
6 5*
-?z
=?-&'
<% i
b/
n y
R £
Room.
Temp.
5 ^5
5Vi
^ V
66
<^> c*
S£
j O
^2.
^ 8"
<£ "?
— .
w* O*
<^. 5-
-------
WOOD IIEATEU CEHTIRCATION TEST
TEIIPEIIATUUE Alll) I:UEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client A" PA Run f /)
Test Fuel Charge
. Page 7, of ~L.
Date
~ 2 5 - S *)
Wood Heater Model ("C- /To Coal Dcd
ES Project. * R P ~/23 Operators
i
u>
I
Time
Sampling/
Clock
-Ll^o
-L -~L ~*> o
1 •*, 1*1
Test
:uel
It.
(Ibs)
-2. .9
o.<\
O,-(J
Fl.ue
Draft
(fn
l?«)
.t'Vl
,
<>9o
'
t(
t»
Comments
~L~l ff f-iif^. Ci..t~s} ~7i> f'l'l j) *
"7- f f- fj
'
Combustor Temp.
// 5-y
r> 2 S'
"?//
•
Surface Temp.
lop
Hear
bottom
17 .S
^9V
Vof
111 ght
Left
Stack
Temp ,
V7?
^75-
V5r,
Oil.
Tun.
Temp .
-------
ENGINEERING-SCIENCE, INC.
Hood Heater
Date //- 2'
SAMPLING DATA
^ /So
Sampling Locat i on C ^
Start Time
Stop Time
Sample Type "2. -5; / ^ 6-
Run Numbe r /) - ~t - /
Operator
Probe Length andtype /•y"
Pi tot Tube Coefficient '-. V
Assumed Moisture
cl
Ambient Temperature -
Barometric Pressure
Static Pressure, (Ps)
Filter Number(s)
Meter
Sample Uox Number /)
Meter Box Number /l'^
Meter II
Ted,
Pretest Leak Hate j_
Post Test Leak Rate „
t> *•
9 *y V7
Read and Record All Data.Every
Minutes
Clock Time
Sampling (24-hr
time.min Clock)
O rL^o
/< 14
If CTJ
b'-T K
/ f 1 ~^> ^O
-> f f/<
°lc OO
t«f 1C
no f-f *a
i 7 f t-J C
/ /& C/~&
Its is
l^o I
» r^/ ^
c ^ V)
P rv <-/<$
* (:' 1 /
o r>S 1
- "^ 1
» d 4 Sf
Ori fice Pressure
Dj fferential
( H), in. H?0
Desi red
, 6 V
Actual
4 t^1 /
. 6 ')
< f~ 1
< c •?
/ (. ~)
, A -7
e ('•O
' ^ 1
. 6. 7
. A 7
fC- 7
. GJ 7
<•
. -.
TEMPERATURES
Di lution
Tunnel
/$
Meter
In
<} :
/„ C]
S 3.
1t-
Lo..-= j
Meter
Out
<* /
(f{/
(* 1
4 /• A
4<-
7-7
9 o
^=»= —
Filter
66-
Implnger
A/V •
6 "3 ^ T
<<. / v*7
A ^ ~ y ^'V C"7
/y /^t f o y O
6 T. i/ e
7y 5/
— » ^» ^=~^ —
Pump
Vacuum
1n . Hg
"$
•5
"^
/?
-^
>3
•^
— =^r
Flue Draft
in. H20
V'.T'Tl-, Tt™ /•
— .
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.
Hood Heater /ffi
Date //- '
Sampling Location Cs^f Tec/
Sample Type <; (Z-
P2?
Run Number /) -
Operator tf,\ < /)
• \Clock Time
Samp11ng\(24-hr
time, m1n\Clock)
"^TT— —lX3o
^7$ • W
3e)t> oo
^e>6 / 5
^20 /0 77. ?"o
/,/ 5 ^5
/ ?/-y ^-c-
<:.V^" /^
/-r^^.V^ 7y-7
^oH^
, r"-/ "JT,
• oy^
, r ; <-/ 1
»^v x
i 0<-/ "7
" <° '•("I
j; n «/H
o f. <-/ 1
c o <•-, V -7
-» «/ ,-S
- o V tt
)ri f ice Pressure
3i f ferential
(All), -in. ll?0
Desi red
-
Actual
. f., ~)
*6 ")
.6 7
• 6 ")
,^T
,^-7
.6">
/£-7
'/& 7
,/, 7
, C- ">
. I ~>
, (, 7
<
' <• ~>
« (^ -)
, /. 7
, ^r '7
. /• -)
TEMPERATURES
Di lution
Tunnel
Meter
In
^S
£7 T,
Z.
K ilter
7T
•) ^
7
I
u>
I
-------
-3-
Date
FUEL MEASUREMENTS
&fj. '(
Project No. p,^ i 7. ~S
Run No. A - "^ - (
^ _.!.• ^
Circle One: /Pretest FueJL-
Fuel Type and Amount* ttT
Ideal Load Weight
Fuel Piece Lenqth ^- G "
Moisture Meter Calibration 12%
Wood" Heater Model Co i ^O
^ x Test Fuel
\y w 1*4
Actual Load Weight
1-7. o 225 z_l. ~7
Moisture Content-(Meter - Dry Basis)—'
Piece No. Readings Average
2
3 __
4
5
6 .
7
9
10
11
12
13
14
15
16
17
18
19
20
Overall Fuel Moisture Average
H-A-3-1-12
-------
A-v/
FUEL MEASUREMENTS
Date //-2& -5*7 Wood Heater Manufacturer
Project No. A-3 - / , Wood" Heater Model CC/-gg
Run No. \
x "N
Circle One: Pretest Fuel Qest_Fjje>'
Fuel Type and Amount 2x4___Z_____ 4x4 "2_ 1x4
Ideal Load Weight .Actual Load Height,
Fuel Piece Length i-j'> .
Mofsture Meter Calibration 125 / 7.. o 22' Z/.~7
u/«cd r< m?. °F - : :
-v^l
. i6'^
^,^* T-
)t»t
Moisture Content- (Meter - Dry Basis)- Cor/*ec7t ., 21,'/
3 l^,g iB.7 l£3 ~\^^ ' IC,.1_
4 HL /f;7 z<5,o /9».3 HA
5 J3.( zc./ ZO.O 1_(. f
& Z5a 12,s LS,1 . IV. 5"
7 7.0.L /-U>?.S /9,7 _-
g "2-ai( j'-l.C- /S'6-" /7. V /-7
9
10
11
12
13
14
15
16
17
18
19
20
v^O
— — ~— ^
^~»-
Overall Fuel Moisture Average
7. A
H-A-3-1-13
-------
TEST
A-3-2
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume' Calculations
PC
I
y*
i
OJ
tO
Stv manu: ORVILLE
Model no: CC-150
Lab name: ES/CB
1st date: 11-29-89
Run no : fl-3-2
Tst time
(«in): 621.00
Chrg ut
(Ib uet): 29.40
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
621
vel dp
(mm H20)
(in.H20)
0.043
0.043
0.043
0.043
0.044
0.044
0.042
0.043
0.042
0.042
0.042
0.042
Units l=metric,
2=English:
Y, DGM:
Pitot co:
Gas Mil :
Pb (mm, in. Ho,):
Tunnel area (m2,Ft2):
Wood moist ('/. uet):
Burn
tunnel
temp
(C,F)
95
102
92
89
90
98
101
97
101
94
99
102
OGM
rdg
(m3,ft3)
925.222
956.800
983.800
1020.700
1052.600
1084.600
1116.500
1148.400
1180.200
1211.900
1243.700
1255. 152
OGM
temp
(C,F)
82
85
85
86
88
87
88
88
87
85
83
84
Samp vol
2 (sin3,scF)
0.995 232.480
0.99
28.56 • Flou rate
21.87 (dsm3m,dscfm)
0.1963 129.44
17.95
rate (dry kg/hr): 1.06
DGM dH
(mm
(in.
0.
0.
0.
H20)
H20)
670
670
670
0.670
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/min)
992.61
998.85
989.92
987.23
999.55
1006.80
986.29
994.40
986.29
980. 12
984.53
987.17
PR
(.'/.)
100.6
99.0
99.0
99.3
99.4
99.1
100.3
99.8
99.3
J01.5
104.9
85.49
17.640
460.00
1850.00
••
dOGH
vol
(m3,
22.
22.
22.
22.
std vs/VmTs
ft3)
415 0.01
589
519
477
vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
991.15 96.67 85.67
22.466
22.
22.
22.
22.
22.
8.
436
395
325
296
448
114
-------
ENGINEERING-SCIENCE INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT CAINS •]- :''-
DATE DEPLOYED //- 1cf - 8 *? PROBE Q , 7
LINE _
CONDENSATE_
TEST LOCATION^/
DATE RETRIEVED//- 2 ?• 5 9
fr/ /?c 77V FILTERS!
SAMPLER SNi? " - " '
RUN*
/,
TEST TLME_
STOVE ID r
(HG BAROMETER UNCORRECTED)
PRETEST B.P Z2--6° (IN HG)
c.i.^5 (—IN HG) TEMP. LQ (C)
FILTERi?2 _ —
TOTAL (MG)
TORR ABSOLUTE_
POSTTEST B.P.
(IN HG)
TANK
\^o
(—IN HG) TEMP.
(C)
TORR ABSOLUTE "7 "7o.- I
WOOD SPECIES /}*c.r /^_Q
WOOD MOISTURE (Z DRY) L/^S_
WOOD MOISTURE (7. WET) _
WOOD CONSUMED (LB) I'M (KG)i'
SAMPLE FLOW RATE PRETEST
(ML MIN)
POSTTEST
ROTAMETER
PRETEST LEAK CHECK
START (3. e (IN HSO) FINAL 6, ^' (IN H20) LEAK RATE 0, L (IN H20 MIN)
POSTTEST LEAK CHECK
START 5, 2- (IN H20) FINAL_f_£_(IN H2) LEAK RATE 0. 2- (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02W 9,80
cog) \M
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT .
ES PROJECT
HUN No. //XT-A3-Z- Placed in Dessicaior: Date/Timej£.
STOVE MODEL No. CC-
POSTEST
'
• WT 1
WT 2
WT 3
WT .4
FINAL NT
TARE WT
WT GAINED
DATE /TIME
IT.-* <>V<;
/2-/ @> /*>cn>
/i-3-S'i
FRONT
FTf.TRR II
5%r--g^
o /366
• I'i&k
-
« /5^
«/Z70
«tf/V4
BACK
FTf.TKR II
5/f^"- ?o
* /2/i
- «Mo9
* /2*9
v/Z/6
"" tffuzT}
CALIBRATION WT.
WT AMOUNT =
PRE WT
fl 5"£^«»-c
* JO fit''
POST WT
» 5^>
I
U)
ro
I
CO
(A)
(13)
-------
CLIENT £
ES PROJECT &£> ^Z 3 STOVE MODEL No.C-C- /
POSTEST
PARTICULATE WEIGHTS SUMMARY Page of
RUN No.!^Ci/2rJL_f?- Placed in Dessicalor: Date/Time ,//~ J>C -gf
Acetone Lo'L II /// y x
Acetone Sample Volume / r>
/V
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
/Z-/6? n6o
O.-l(S /f/5"
fl-t-n
t ^C
HEARER II
/)- ^^>
~?<3< "*> Ka5
7X, -3SoV
")$• T><*-Oft
' ~1 S.3f?9
o o 3 /I
CALIBRATION WT
WT AMOUNT =
PRE WT
*>0 , C<'C> /
<^o,Cstx, 7_
POST W'l1
^o ,c<>ci "L.
So .ova/
ROOM CONDITIONS
RELATIVE
HUMIDITY
/* <®47.
/f^sr
BAROMTRC
PRESSURE
-L.t.V
i-/< X
Initials
/*<#'
W'e/l
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAU PARTICULATE CATCH (A-i-B-i-C) =.
-------
.CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY ' Page of
RUN No.^j- "^'"? "?: Placed in Dessicatox-: Date/Time //" "V f$7
/2'5 STOVE MODEL No. so7L
*>&,&&/
ROOM CONDITIONS
RELATIVE
HUMIDITY
/ 8 ^ 7
/t&tiK
BAROMTRC
PRESSURE
I/,*?*
I/, %
— TS~
Initials
/*c4'
i**<=/{
I
OJ
I
to
(BLANK CONC.) x
(ACETONE SAMPLE)
WT GAINED
(C)
a oo*l>V
, 3 Z / 7
TOTAL PARTICIPATE CATCH (A+B+C) = 3V3«9
_'nti.
-------
CLIENT _L
ES PROJECT /? 0 /23
PARTICULATE WEIGHTS SUMMARY Page of
RUN No. A"~^' Z. Placed in Dess icator: Date/Tiine_/t£5L!
STOVE MODEL Mo. C^C - / ^G
POSTEST
;
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
it- / &/t>$&
(2_~/ (9/825
//-3-8<)
FRONT
FTr.TF.n II
A£-&~?
/f tnpt'Cj
-999-?
.999-7
-s^'^So
*3z;7
BACK
FILTER II
A£-/6S
.•£*7y
^7?y
«^7/
«67S7
,^^V
CALIBRATION WT.
WT AMOUNT ~
PRE WT
/ 'TfrCt
* ^OC' &
POST WT
t £ t'C'O
-V75")
ROOM CONDITIONS
RELATIVE
HUMIDITY
/'S&6,'}
/9&>6>&
BAROMTRC
PRESSURE
It'V
•?-/, &
Initials
I
/?• C4
Sk^SZ
(A)
(13)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' Run t
3*7
ES Project 9
Wood Heater Model
Operators
C.C /5"o
K*
TEST RUN INFORMATION
Attempted Burn Rate
Achieved Burn Rate (Kg/hr)
Primary Air Setting I '/Z
/
Secondary Air Setting A/o
Thermostat Setting_
Other Settings at,
/VA
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (SF)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
'!/, *? /
u^>
3
1 O
/t.c/ic>.0
Hl^l
rto~t~
Post
Test
Z-l -8 H
V/
/T_
C"
jn.r, ///< C
/
- / c
-57
TEST FUEL DATA
to 1 1. 7
'
Actual Fuel Charge Wt.
Coal Bed"Range Wt.
Actual Coal Bed Wt.
Fuel H2(K Dry _£
Fuel: Dry Kg
to
Z,
Wet
C . Ci
LOADING/TEST START OPERATIONS
By-pass oO'^ v
Door f\~cr *>y<-/'
j,r 5^>- Air Settings Q>^
•fc,<- 5"-^'— Comments
*ox tr 6--
Veloci ty traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
H-A-3-2-7
-------
-•v
ENGINEERING-SCIENCE, INC.
Clientp p/V Run
WOOD IIEATEU CEIlTIRCATIOII TEST
TEMPEIIATUIIE AMD |:UEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page
Date U-T-^-B*} v/ood Heater Model <^c f'° Coal Bed J . 7_
ES Project 1
'line
Sampling/
Clock
o~7(jc>
67/5
07V 5
£'%xDC>
£><& i S
DfToO
oLioo
Jo ofj
i! "^
(7-^0
/l^o -
/"-/d>O
/6^0-y
I'^'^'i
1 6>6O
/ -7£> c^>
£"> /*v/-S
/ (5 t-'LX
/ / t/^&
fl ~L 1
i
Test
ruel
n.
Ibs)
'/• 2-
7. "^
O-S
7-1
3-V
C7,cj
y*^
/c %
0.3
•cf, 0
H-C7
1 « /
L/ ^
y. /
/. "7
^ _ ^
Fl.ue
Draft
(in
6,661
i^.o^z.
, '^"7
"
ftt)l'2-'^ Operators (>J^^ v.\Hc^
Comments
j\ojp C \'**(\t\P' "( c\_^"\ t ""-* p£(f'ff2\
" ^~~y\ \\ 'v^£?V llrvV" C\' l^^-^-i
Ai*7^'l/°'i s •• A » ^ t* \ ^ \ ^M~f VNO'-X
j
o'T-l~] - R''/^ 8d.>ii (.v^.V's^
\\>s( c, ct'^0p,.((
tjO i i^* • /£> .ii \ (; { \ y ~° * i
^>05S foti.rcQ Po\c,\^
"T^-t>-{- -Mc-r"V
f.3/-.G ^,J' c • '-"<" ^' - '•V ^
Coml)ustor Temp,
1 1 7 t*
<-i i "1
(/IS
/ '^/T1 0
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c// 2-
tz ^
fifi"3)
(i>/ Z-
t\LcLl
III'1'
' >i',- '•?
l'l~7
'3 -' 1
^7 7
-?//
Surface Temp.
lop
Hear
Dot Loin
~iclO
3V 2-
Lta(
-T'cifi?
7>'>^
V27
•y/7
tight
Left
•
Stack
Temp .
737
(J.|(Cj ^
7/S"
79 c,
^'x 'Z-
% 2-
j^o_2
.77*^
t^l 7
^-7^,
..v?
t-fie't
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^i~!
1 0 /
Vy
99
/yi 7
loom.
Temp .
7V
£j
757
V "5
"70
7 f
7o
£ 9
'l
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type 5'<
Run Number . /4
Operator
Start Time
Stop Time
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter 6 .
Probe Length and Type_
Pi tot Tube Coeff1c1ent_
Assumed Moisture
Sample Uox Number
Meter Uox Number ^
Meter H
il /
/I'..
Pretest Leak Rate o.oos
!^
~?c>
Y'?
ft f*\ / A o *^
-7S
/a^
/ 2.O //£O
/ "i*> /<
/ ^C> 1(0
/ os yf
; g0 /-£ c^>
/ t/C /•$•
7 yo 3<^>
-? 7^ V "T
i V
"?y<" /^
33o ^^
~~li-fC '-I <~
^4c? / C » ^
,
/AZAV
/(•-, ^Z Y,
76,^ */ .fjt-f-l
•^ nQl^
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,67
4> 7
7
9 o
• ^ ~7
c)&
Meter
Out
vl-> T
S 5"
S *T
fn;
b-'^
ft~7
r\ J
Filter
~7 "2-
•
Impinger
A, / •
7^ •T^T
7S ^7.
76 ITc,
7ft "5"^
7 ft VV
Pump
Vacuum
in. Hg
-^
^
-5
3
"^
V/ ^^i 1 ^
Flue Draft
in. H?0
PG
I
>
I
OJ
I
N)
I
VO
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
V/ood Heater
Date /
/) -
z
Sampling Location_
Sample Type_
Run Number
Operator
_A_
• \. Clock Time
Sampl1ng\|24-hr
time, m1n\Clock)
~fC7^ -£S£Q_
-3~7^ • )S
I'Jn If
^^ V*5
y?& >/«co
V?5" /T
V^ ?o
-^T V^
V
4/^6^" / 6
^a -?o
^7^ V6
^V<9 /5»^
4^5" /^
^7c? 16
T'?:;^ V^
//>^^ y^
(<>/<; i$
ffi.l <. o*-/ 1_
d'.^V^
o-/^
.O'V -i
o^-S
oV5
.Wi*
.&VZ,
.o«y 2_
o*y/
-0L/|
,6-y L_
,o<~/^_
.e>L/2-
. « Vl_
f ^>V1_
.f.^l-
. O'f V
Ori f ice Pressure
Di f ferential
(all), -in. ll?0
Uesi red
Actual
.ic~7
• <7
, (o 7
>(o~7
.(,-]
,G -1?
.^-7
.67
>(,7
.d>-7
•t-7
»^ 7
. /;-,-?
, /, ')
, An
TEMPERATURES
Ui lution
Tunnel
leter
In
f?V
ftf*
o 5>
-^C
-
Me t e r
Out
e.;>-
iS7
O'..
C.J ->
-£&—
t, T,
f>^
:ilter
«G
Bo
76:
-VA
?b
S/
Impinger
;rft
^ /
-T V
->'
^>
>
"-t -
"S
^
Flue Draft
in. H?0
PC
I
>
I
LO
I
-------
FUEL MEASUREMENTS
• A-3-Z
Date ('' <^"^>~\ Hood Heater Manufacturer /]/V,H
Project No. AS? D! ~L ^> Hooo" Heater Model Cc i "5CJ
Run No.
Circle One: (fPretestFjie-l • Test Fuel
Fuel Type and Amount 2x4 \ / 4x4 1x4
Ideal Load Weight ; .Actual Load Weight "
Fuel Piece Length ^ C-,-
Moisture Meter Calibration 121 ' 221 ',
Moisture Content-(Meter - Dry Basis)—1
Piece No. Readings Average
. r-iz> V3 ? /Q 7 /A5 d C?
1 hi / /O / / / (c-'-o O
2 __
3 __
4
5
6 . '
7
8 _
9
10
11
12 .__
13 .
14
15
16 •
17
18 •
19
20
Overall .Fuel Moisture Average
H-A-3-2-11
-------
FUEL MEASUREMENTS
•A-
Date
8 ?
Project No. A
Run No. 'A- ~
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight '
Fuel Piece Length'
Wood Heater Manufacturer^
Woocf Heater Model c"T / •
4x4
i lC
(?
1x4
Actual Load Weight
Moisture Meter Calibration 125
\Jvf
-------
TEST
A-3-3
-------
Method 56 Proportionality Rate, FIoo Rate,
Burn Rate, and Sample Volume Calculations
I
Lo
I
OJ
I
Stv manu: ORVILLE
Model no: CC-150
Lab name: ES/CB
1st date: 11-30-89
Run no : fl-3-3
1st time
(mrn): 600.00
Chrq ut
(Ib uet): 32.00
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
vel dp
(mm H20)
(in.H20)
0.040
0.041
0.045
0.042
0.040
0.041
0.041
0.042
0.041
0.042
0.042
Units 1 -metric,
2-English:
Y. 0611:
Pi tot co:
Gas MU :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Hood moist (.?. uet):
Burn
tunnel
temp
(C,F)
108
103
100
92
10?
108
104
98
106
96
93
DGH
rdg
dn3,ft3)
256.015
288.500
320. 300
352.000
383.700
415.700
447.700
479.800
511.500
543.600
575.643
DGH
temp
(C.F)
91
92
90
83
83
95
96
91
89
86
86
Samp vol
2 (sm3,scf)
0.995 222.627
0.99
28.56 Flou rate
21.78 (dsm3m,dscfm)
0.1963 126.80
17.52
rate (dry kg/hr): 1.20
DGH dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(iTi/min)
(ft/*in)
970.51
978.23
1022. 10
980.37
969.65
982.56
979.10
985.68
980.83
983.91
981.25
PR
a)
103.
99.
93.
101.
103.
99.
99.
99.
99.
99.
1
4
8
8
1
8
2
6
9
4
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
22.
22.
22.
22.
22.
22.
22.
22.
22.
std vs/VmTs
ft.3)
589 0.01
072
083
368
373
091
120
043
402
vs ave tunnel DGH
ave temp ave temp
(C,F) (C,F)
983.11 101.36 89.73
22.485
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED //- 3'
DATE RETRIEVED | f ' 3°
TEST TIME IL
TEST LOCATION CZB
SAMPLER SNJ
(HG BAROMETER UNCORRECTED)
PRETEST B.pZ-f.^O (IN HG)
PROBE •"==• ft f- 'RUN#
LINE _
COMPENSATE "2 7 e .
FILTERS y^,9 STOVE ID CC/50
FILTER;? 2 (IN H20 MIN)
POSTTEST LEAK CHECK
START 5,(o (IN H20) FINAL ^'V (IN H2) LEAK RATE £• Z, (IN H20 MIS)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
CO(Z)
02 (Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBS+FITTING
SAMPLE LINE
CONNECTOR
MIN.
MIN.
H-A-3-3-2
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
_of.
CLIENT .
ES PROJECT
/Z~\
RUN Ho. t)/>T~/)-3~~*> Placed in Desslcator: Date/Time //- 3
/Z-/ & /9*&
i/^-t']
'
FRONT
PTf.TKR II
5^9/-?5
^ /376
*/375"
. *17$
*/lo6
• o/£>q
BACK
FTf.TRR II
.5/fcf- 9<^
• /ZI6
'/2./0
o/T. I (p
-/z/y
*c>-c-o 5
CALIBRATION WT.
WT AMOUNT =
PRE WT
£ £<:•<:•£>
y ?C><3 <^
POST WT
^ 5^co
/ 5crt'-&
ROOM CONDITIONS
RELATIVE
HUMIDITY
/6^67
/
I
CO
I
Co
I
CO
(A)
(B)
-------
CLIENT .
M
PARTICIPATE WEIGHTS SUMMARY Paye of.
RUN No.I)/J- ~/>' 5" 3 Placed in DetisicaLor: Date/Time.
STOVE MODEL
Acetone Lot. (I *?// &
POSTEST Acetone Sample Volume
WT 1
WT 2 .
WT 3
WT' 4 .
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
* — .
12- /(^ 17 to
jl~ //„ g ^
HEAKER II
7V.3^9y
7/r 369T
7V. 3^/5-
7V, 33C/^
. c? Z97
CALIBRATION WT
WT AMOUNT -
PRE WT
£- ^ ^ ^
$o.c**-L,
POST WT
SO, i'T*' 2_
So.fvol
//} ^/
ROOM CONDITIONS
RELATIVE
HUMIDITY
/&&&•?. '
/
I
U)
I
u>
I
-p-
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICULATE CATCH (A-i-E+C) =.
-------
Page.
_oJE.
CLIENT
JEM
PARTICULATE WEIGHTS SUMMARY
HUH No. Q6- '/I' 3 3 Placed in Dessicator: Date/']'i me / Z - /- g'l.^g•]
ES PROJECT /?/? /Z3 STOVE MODEL No. J±:£Lj
POSTEST
Acetone Lot II
Acetone Sample Volume
•
WT 1
NT 2 .
WT 3
WT 4 .
WT b
FINAL WT
TARE WT
NET
DATE/TIME
n-i (& n$o
H-/& /<7/5
//-^^
WEAKER II
/9-7V
79^ 061*5
1^'Otf-L^
77*00-1 ^
-77.0 , cnr't 7
POST WT
£c, ti-a'L.
So .frffC /
ROOM CONDITIONS
RELATIVE
HUMIDITY
/6<^>7
ft® 6*
BAROMTRC
PRESSURE
-L/
-------
CLIENT .
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page of.
RUN No. n ~3~ 3 Placed in Dessicator: Date/Time.
STOVE MODEL No. CC ~ / So>
POSTEST
;
• WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
) ^ - / & n s $
/2-/(9/6V5
f/- 3 - S> °l
FRONT
RTF.TF.n II
ft£-ni
/. a^o
I,6WO
{•otfto
*£-)vct
-y/y/
BACK
FTf.TER II
/l£ 17$
• 6
-------
Client
Date // -
WOOD HEATER CERTIFICATION TEST INFORMATION
£ PA Run I A - ^ '
- 8 -7
ES Project t A D /Z
Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (fcfAr) ///<; t, Secondary Air Setting _|v
Achieved Burn Rate (Kg/hr) 1, \°[~j Thermostat Setting
Primary Air Setting />•? ft x
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
2.
/6'0//0, 0
^C-5
^).CC>O
Post Test
ZX. 75-
(^ <^'
/ 7
(O
// . "//d ,C
3P/7
, 78
TEST FUEL DATA
to
Coal Bed Range Wt.1
Actual Coal Bed Wt.
to
Actual Fuel Charge Wt.
'
Fuel H20% Dry I'/, £<•/ Wet 1
Fuel: Dry Kg f I, C( 1 L-
LOADING/TEST START OPERATIONS
By-pass S^ ^T V ^/^ Air Settings
Door S£> .,7 4^ /*^ / *j Comments
Yeloci ty Traverse
Temp
Ave.
2 ^
3 ,
4 ,£3.2
Pitot Leak Check
H-A-3-3-7
-------
A-3
WOOD IIEATEU CEItTI F [CAT ION TL:ST
M mun
s__??
sw~
W«nJ
TEMPEIIATUUE AND FUEL CONSUMPTION
ENGINEERING-SCIENCE, INC.
CHunt C/V? Run # // - ?, - "? ' Test Fuel
DATA SHEET
Charge /ex 7 //, 3
Date //- '$&-'% ^ Hood Neater Model Coal Bed ~2
ES Project 1
1
i
t
ii
i|
I
PC
1
1
U)
1
1
00
"line
Sampling/
Clock
f3^\5c)
lYJ ZC3
r>c)3o
O '"Y ^
jlT&V
la J ^
Id ~*,C'
/o y^
// £f>
///<$
/? / *7
y "?/ ^
/ 35 "iC
/ ly (rf)
m /^
1 *-> T^
Iff /s
/7 / <"
> 7 "1 1
^',^_
Wy ^
Test
:uel
Ibsl
^.S
/.1r\
16,0
"fi.^
7.T
y«"?
?- /
/O,"7
^ ^7
/o
C7^<^
//« ^
ki'C-
£> > 3
/, .c,
X7, "^
fl*C>
/O e O
fe
id^
Fl(ue
Draft
in
o>Q^A
tf>t-li>
&1/3
,0^5
oO'xi
o^.'^y
^^•^b
o.^7
^ /N cA ' i-"1 f • -(\i"e t't~
'/£./,?> I/^D4* A/iMr'-A' ;vi(.^-,(
<'i,r- I^'J-K
2-,"^x'g'(W
Surface Temp.
lop
Hear
liottoiii .
i^-o
? <- 7
r?c? "Z-
•rt 7
*-/& *>
vv/
?&¥
L/y&
--/ 7 <*>
y 5*7
v?v
^^2___
Kiglit
Left
•
Page J_ of
Stack
Temp .
*{<-'<-/
V"? V
?79
^"'V
•57Z
3? 7
^ 2C
•-"5" 2.
ty^y
vf,y
vl^
on.
Tun .
Temp .
V^~7
S, ^
97
^
5"
<^ *T
<^^"
^ ^j
fag-
<^-9
-7 -^
7 1
<£ 7
J^-
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
-3
Mood Heater
Date //- ~*
C ~
Sampling Location V?,.
Sample Type
Start Time
Stop Time
TTPT-
Run Number /?- ?- 3
Operator
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter o 99 5"
10 H
Probe Length and Type . /y --
Pi tot Tube Coefficient .97
Assumed Moisture 4^ */Vj
Sample Box Number_ ^
Miiter Box Number /fr
Meter H
Pretest Leak Rate
Post Test Leak Rate
*. * r-i
f>
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
time.mln Clock)
0 HI?
3cj (/$
vr
J2 o ) % / 5
/ ?5 3e>
/ Go VT
y/S?" ero
I $Q ft)*
1 & £~ *^i&
2>o V5'
1Yo 1 *> /5
2 T^ ^
^?7o Vy
•Z 3*7 *""£»
^ ^ / /?. 75"
1^ V5
2»^ / 7 / 5"
Gas Meter
Reading,
(vm) ft3
-2S5, ^
•3 ZiTJ,, ^
.
7^"? ' ^
"? *H ^ ,1' /
'V/^'. "7
VV 7 .» 7
Velocity
Head
( Ps), in.
H?0
* ^ Vf :•
, t-l £>
A^) H "5
» c>Li ^
• * O V^)
» o -VS"
-<^ V 2
„ o^V ?
»« ul f>
/> r> V/j
•
'67
, ^ -7
'
. "7
?.> 7 ^;t'o
Pump
Vacuum
in. Hg
^
^5-
^
<^-
5
S
^
Flue Draft
1n. H20
33
I
>
I
U)
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater
Date //- ?
Sampling LocaUqn
Sample Type
Run Number ,
,<> f s
«
- 3- 1
Operator /i, t
"X. Clock Time
Samp11ng\(24-hr
time, min\Clock)
• 'TT^TT— — ^l£i_
*V7T • ~*,a
-T.IO Y5
VeS tf.>
^70 !*,!<=>
V?< TO
IV<5> VT
V6T ^/t*
VJ^ /? /5"
W I''
4»D v^
^V6 ?^>/^
Gas Meter
Readi nq
i^vLliL
^
V7-/-5
^y/, ^
yy7-^
L/2.
• v-11
.o?l
t>V 2-
_10L<'/
,ovz_
. ^"-//
,. tfV/
-oV -3
..^v •?
* <-JV 7
^ -7
•
-&->
, 6-7
. {< -)
.^1
'&• •")
,^9
TEMPERATURES
Di lution
Tunnel
Meter
In
Vtf
9^
5?f
97
-
Meter
Out
V/
f-40
3-6
£X
Filter
6'^
S V
79
7tf
Impinger
rT77
->'
-T
^T
<
"*"
Flue Draft
in. H?0
CC
I
I
LO
I
-------
FUEL MEASUREMENTS
Date
Project No.
Run No.
K N I
Hood Heater Manufacturer
Wooo" Heater Model
C.C 15
Circle One: Pretest Fuel • Test Fuel
Fuel Type and Amount 2x4 "2— 4x4 "2-- 1x4
Ideal Load Weight •
Fuel Piece Length
.Actual Load Weight
Moisture Meter Calibration 12%
vJ*«d 'T<~,-a. °F
/L- O
225
19
20
Moisture Content- (Meter - Dry Basis)-
Readings Average
0. V :/.(
e./s
x4.'
^
Overall .Fuel Moisture Average
H-A-3-3-11
-------
TEST
A-3-4
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Pate, and Samp19 Volume Calculations
PC
I
Co
I
-p-
I
Stv manu: ORVILLE
Model no: CC-150
Lab name: ES/CB
1st date: 12-1-89
Run no : fl-3-4
Tst time
(min): 570.00
Chrg ut
(Ibuet): 32.10
run
time
(min)
0
60
120
180
240
300
360
420
480
540
570
vel dp
(mm H20)
(in.H20)
0.042
0.041
0.041
0.042
0.041
0.041
0.041
0.041
0.041
0.042
0.042
Units 1-metric,
2=English:
Y, 0611:
Pilot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (m2,Ft2):
Hood moist <.?. uet):
Burn
tunnel
temp
(C,F)
99
105
96
100
106
101
92
106
99
%
99
DGH
rdg
(
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED ' Z--/-O*
DATE RETRIEVED
TEST LOCATION (l3>
SAMPLER SN// 9V/&7
(HG BAROMETER UNCORRECTED)
PRETEST B.P Z/-86 (IN HG)
TANK c ('. SO (—IN HG)
POSTTEST B.P. '£2.O'7 (IN
TA-MK "LftO (—IN HG)
TORR ABSOLUTS L "H? .'"I
WEIGHT GAINS
-f PROBE £X-C/
LINE '
CONDENSATE £/, /
FILTER* 1 76,9'
FILTER/2 O t i
TOTAL (MG) *i ^tO
TEMP. ^3 (C)
HG)
TEMP. ~L\ (C)
RUN* /j - 3 - ^7
- TEST TIME '1,^ (•MJitJ
STOVE ID CC / 5 &
WOOD SPECIES ueu^l<-i r'r
WOOD MOISTURE (Z DRY) "3^> ^ ^.
WOOD MOISTURE (Z WET)
WOOD CONSUMED (LB) ""Z,! (KG) *"/• -
SAMPLE FLOW RATE PRETEST
ROTflHETER ^? -'(ML MIN) ^'0
POSTTEST
ROTAMETER % ^ -(ML MIN)
PRETEST LEAK CHECK
START G> . [ (IN H30) FINAL ^^ (IN H20) LEAK RATE , 2- (IN H20 MIN)
POSTTEST LEAK CHECK
START 6-0 (IN H20) FINAL ^ (IN H2) LEAK RATE • [ (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(2)
RUN COMMENTS:
02 (Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE+FITTING 7.- /9V7
SAMPLE LINE
CONNECTOR
MIN.
MIN. +
MIN.
MIN..
../
-------
PARTICIPATE WEIGHTS SUMMARY
Paye.
of.
CLIENT .
ES PROJECT
EPfl
HUH
Placed in Dessicator: n^ l.e/Ti.ne/2- ?
3 STOVE MODEL Mo. C,C / *
POSTEST
Acetone 'Lot II.
Acetone Sample Volume -Ii> "2-
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
\-L-*,@Ml*>
H'T&T./fS
/A4^9
HEAKER II
/? ~ *9 ~~)
7«,^>*> 3£
7 ]4^
(BLANK CONG.) x
(ACETONE SAMPLE) - (-'
WT GAINED =
• <^ / / (C)
TOTAL PARTICIPATE CATCH (Ai-B+C) =
_int;.
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN Ho. /y/>/'/?-3-//Placed in Dessicator: Date/Time /2 - 2 - g 9 ^X t.
/2"^ STOVE MODEL Mo.
POSTEST
1 WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE NT
WT GAINED
DATE/TIME
/2'3^/^Vo
x>.
/2--5
•llt-L
el'l* t
'/^VL
a /Z/^
«0 /6^
BACK
FTr.TKR II
5/7^-^o
* /22.-L
./Z2^
, / Zi-Z-
«/^Zo
.> 0002L
CALIURATION WT.
WT AMOUNT =
PRE WT
t ^060
• vm
POST NT
f £c>*~e>
f 5*v1
ROOM CONDITIONS
RELATIVE
HUMIDITY
/r6%is
fZ®7/
DAROMTRC
PRESSURE
"Z./.9
^A9
Initials
i
/a^/C
/V*:/?
1 "
i
OJ
I
(A) (B)
.»
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Pays of.
RUN No. ^'/?' ^ / Placed in Dessicator: Date/Time.
STOVE MODEL No. PC"/^.^ <}"2,?-_
POSTEST
Acetone Lot (I.
Acetone Sample Volume.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
n^&fii*
i2.--i(&2t?s
//-v^r
WEAKER II
/Q-?«
£L3gS±. o -> -L^c-c.
T> li • > /- 1> C, > ^Ol» /
^ ^.3^6-^
8 2, -35TC-2L
5S?.37/^
C' , <: / V ^
CALIBRATION WT
WT AMOUNT =
PRE WT
&,<**-*.
-
ROOM CONDITIONS
RELATIVE
HUMIDITY
/9^?
lT@~)f
BAROMTRC
PRESSURE
Z/, 9
'T-/^
Initials
XM^/?
/*>/?
EC
I
U)
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
/V3
(C)
/ /
TOTAL PARTICULATE CATCH (A-i-E+C) =.
-------
CLIENT E P H
ES PROJECT HO
3
PARTICIPATE WEIGHTS SUMMARY Page of
x^
RUN No. /)" 3' V Placed in Uessicator: Da J.P./Time ItrZ- *'~i ^>/
STOVE MODEL Mo. CC
POSTEST
v
• WT 1
WT 2
NT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
/Z -3 0^/3 5-$
tl-l&il to
ft -«&/<) lf>
//-3~3r7
FRONT
KILTER II
fc-/53
t'//3<5
/•//Z-L
J.//OC
/ * // ^c«
^67/7
- V3<33
BACK
FTLTKR II
y^-/^
.£ 7?^
•&-)*y
*CflM
• U7(
• 0/13
CALIBRATION WT.
WT AMOUNT =
PRE WT
e *)£>£>&
'V?^^
* ^f>-r /
POST WT
a 5^0 ^
tf ^<--Tl Z-
« 5 ^^^ /
ROOM CONDITIONS
RELATIVE
HUMIDITY
/?<^-S)
I-L&-I!
lo & If
BAROMTRC
PRESSURE
^/,
I
OJ
I
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
• " Run /
-£
ES Project I
r\
Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr) I . 11'"f
Primary Air Setting
/Tw ^7e ri;,-,
v — •' 'w ' '
Secondary Air Setting /yO Cc
Thermostat Setting A/A"
Other Settings jV
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Pretest
Zl.7
OiC-^O
Post Test
2/, ~T=/
70
10
&
'C»C/ /'J.-C^
LfeCf
TEST FUEL DATA
Fuel Charge Range Wt. 9-6; to //. 7
Actual Fuel Charge Wt. ^ "- ' \
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2« Dry "ZC-3Z. yet
Fuel: Dry Kg
to
LOADING/TEST START OPERATIONS
By-pass &{:;-, Tu^S^ni-^ Air Settings
Door /^; v./- *tu i— 5 t^'-- Comments
d
Yeloci ty Traverse
Temp
A 1 C
2 ,
B 1 0.03k
2 .
Ave.
Pitot Leak Check
3 QV7
4 .038
3 05O 9O
H-A-3-4-7
-------
A-l-V
WOOD IIEATEH CERTIFICATION TEST
TEMPERATURE AMU PUEL COM SUMP TI Oil DATA SHEET
ENGINEERING-SCIENCE, INC."
Client epA _ Run I
Date
2,- f-
ES Project I
,
A - W
Test Fuel Charge
Hood Heater Model <-("/•;<•, Coal Bed
Operators (-\jl~\tt ~\
. Page
PC
I
t>
I
UJ
I
00
Time
Sampling/
Clock
Test
Fuel
HI.
15.
9.7
% -7
.•r. z.
7-6,
(O.O
//. 0
IQ.L-
A
_£
O-O
Fl.ue
Draft
(in
M?0)
oyo
^a
Comments
7..o«
l^cr t^t.il-Vj
Combust or Temp.
•77-7
/ Z c' 0
2 -/•=;
lop
Hear
Surface Temp.
Bottom
/.lo
"//o
RfghT
TelT
Stack
Temp .
36 -S
£•*/-> T
5*2
v'/y
on.
Tun.
Temp .
'7V
2JL
TL
to/
Room.
Temp.
V
&
C-7
:Z£L
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
J>
Wood Heater
Date /2~- / '
Sampling Location
/
Start Time
Stop Time
C
Sample Type
Run Number
Operator
S£7
/)-?>-"
Ambient Temperature
Barometric Pressure
Static Pressure, (P^T
Filter Number(s) '_
Meter >(-
Probe Length and^Type
Pitot Tube Coefficient
Assumed Moisture ^7
Sample Box Number
Mater Box Number //-
Meter II
Us-
Pretest Leak Rate £.00' I d
Post Test Leak Rate
O.
*=>
Read and Record All Data Every (:<-> Minutes
Clock Time
Sampling (24-hr
timefmin Clock)
G &i I IS
/*?
JO
HI
(eO /G|<=$ .
75
Qo
/1>S
lio /ic^S
/c;0
19^
-7?(^
£¥G fb'S
•> s"1^
7.7O
X95
"3oo / "-Y/S
TSIS
\-^^
Gas Meter
Reading
(vm) ft3
£07. o
o^ft. ?S
//>/ ^"/ — 7
it'C" /, /
*7<^>C'. (o
-7 3 / . C,
Veloci ty
Head
( Ps),1n.
JijO
O.o"-y 2-
.bVZ_
* <^v/
„<-.•-//
o*V /
i O'-/ |
£,«-/ 1
-OC( ^
,O>'i I
. °V "2_
. . o<-/ ^_
, o1-/ "2-
> °V"i.
. cW Z_
. o •-/ ^.
u^/l
.o<-^ ^
.c?1- 1 '
, ^ *~ 1 (
o^//
^o<-/(
frl-/<~J>
. o^-/ /
Ori fice
Djffere
( H). in
Desi red
k 7
ressure
ntial
H20
Actual
O"7
.6-7
>fr->
L< ~~>
.6-7
• 6 "7
0.7
.6^^}
.6-7
.0-7
,07
.(0-7
.0-7
.c- 7
/• • ~i
1 ^f* ,
• ' 'f ~~i
.6 7
, ty
• I .-- "7
, C. 7
'^/7
TEMPERATURES
Di lution
Tunnel
Meter
In
7 'S
8 /
£f~>)
SLI
•ft1-/
'fVS
.^.* /
Meter
Out
"7 ^
n >
^/
B /
?• "i-
S c/
-^ '• O
Filter
/' ^J
•
Impinger
6p 'S
^ -> i - -,
(f-lL, ^>" C-
(^"2- S" V
^ "i- c.' (
<:j c/ 6 ' a
^-. -,-•,
Pump
Vacuum
in. Hg
— ?
-x
-^
-\
"*-)
~\
---,
Flue Draft
1n. H20
w
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater_
Date
o
^ - / -
Sampling Location
Sample Type fi
Run Mumber
Operator ,_
Tf
• \. Clock Time
Sampl1ng\(24-hr
time, m1n\£lock)
. ~ — — _.
^V7S
TS
yts -z,n
b (/ 1
. r-Vn
a S< V 1
o ef'^j /
.QH(
.0
6 o
c'' r-
6-.V
•
}ump
Vacuum
in. Hg
1
^
3
^
Flue Drift
in. H?Q
j
. ]
! :
\
I
I
i
I
i—•
o
-------
,^
FUEL MEASUREMENTS
Date
Project No._
Run No.
Wood Heater Manufacturer
Wooo" Heater Model
-------
APPENDIX I
PROPORTIONALITY DATA AND ALL RAW RUN DATA
FOR THE AK-18 TESTS AT CRESTED BUTTE
-------
TEST SERIES
B-l
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sanple Volume Calculations
I
ta
I
Stv •anu: SWEET HOME
Model no: HC-18
Lab name: ES/CB
1st date: 11-9-89
Run no : B-l-1
Tst ti«e
(•in): 720.00
Chrg ut
(Ib uet): 30.80
run
tine
(•in)
0
60
120
180
24)
300
360
420
480
540
600
660
720
vel
(M
(in.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
057
053
055
057
055
057
0.052
0.
0.
0.
0.
0.
0.
052
053
054
054
051
054
Units l=netric,
2=English:
Y, DGM:
Pilot co:
Gas MM :
Pb (IM, in. Hg):
Tunnel area («2,ft2)
Hood «oist (?. uet):
Burn
tunnel
te«p
(C,F)
59
67
85
92
92
93
91
.86
85
79
87
89
84
DGM
rdg
(•3,
18.
47.
77.
107.
138.
169.
200.
231.
261.
292.
323.
354.
385.
ft3)
003
400
500
900,
500
100
100
000
800
700
700
500
006
OGM
temp
(C,F)
57
69
82
87
89
91
87
85
84
81
81
84
79
Sanp vol
2 (s«3,scf)
1.009 263.630
0.99
28.56 Flou rate
21.80 (dsa3m,dscf«)
0.1963 147.15
11.76
rate (dry ko/hr): 1.03
OGM dH
(M H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(•/•in)
(Ft/»in)
1106.92
1075.57
1114.23
1141.57
1121.36
1142.60
1089.36
1084.41
1093.78
1097.96
H06.08
1076.88
1103.04
PR
02)
97.3
103.6
99.9
97.2
98.8
97.5
101.8
102.1
100.6
102.6
101.6
101.8
dDGM
vol std
(•3,ft3)
22.113
22.128
21.812
21.755
21.676
21.879
21. 968
21.978
22.090
22.284
22.140
21.808
85.49
17.640
460.00
1850.00
vs/WTs vs ave tunnel DGM
ave tenp ave teap
(C.F) (C,F)
0.01 1104.13 83.77 81.23
-------
Method 56 Proportionality Rate, Floo Rate,
Burn Rate, and Sample Volume Calculations
Stv aanu: SWEET HOME
Model no: FttC-18
Lab name: ES/CB
Tst date: 11-10-89
Run no : B-l-2
Tst ti«e
.(•in): 720.00
Chrg ot
(Ib oet): 22.80
run
ti«e
(•in)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(M H20)
(in.H20)
0.065
0.058
0.056
0.058
0.057
0.056
0.060
0.058
0.058
0.058
0.059
0.058
0.057
Units l=»etric,
2=English:
Y, DGM:
Pilot co:
Gas MW :
Pb (ntrn, in. Hg):
Tunnel area («2,ft2)
Wood moist C/. uet):
Burn
tunnel
(C,F)
80
95
100
%
92
87
84
85
82
85
85
87
r 89
OGH
rdg
(«3,ft3)
386.
416.
448.
478.
509.
403
800
600
400
600
541.000
572.
602.
633.
664.
695.
727.
758.
100
800
600
600
800
100
285
DGM
temp
(C,F)
74
81
90
90
88
86
83
84
84
83
85
86
83
Samp vol
2 (s«3,scf)
1.009 265.862
0.99
28.56 Floo rate
21.82 (ds«3«,d5cfa)
0. 1963 152. 13
11.72
rate (dry kg/hr): 0.76
DGM dH
(M H20)
(in.H20)
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(ft/«in)
1205. 17
1154.13
1139.16
1155.17
1141.04
1125.86
1162.17
1143.69
1140.54
1143.69
1153.51
1145.78
1137.94
PR
96.6
105.1
97.4
99.9
101.2
101.4
97.7
98.9
100.3
100.9
100.4
100.8
85.49
17.640
460.00
1850.00
dDGM
vol std vs/WTs vs ave tunnel OGH
(«3,ft3) ave temp ave te«p
22.
22.
21.
22.
22.
22.
22.
22.
22.
22.
22.
22.
(C,F) (C,F)
157 0.01 1149.83 88.23 84.38
880
090
081
303
171
007
038
181
366
355
232
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
Cd
I
to
Stv nanu: SIEET HOME
Model no: RtC-18
Lab name: ES/CB
1st date: 11-11-89
Run no : B-l-3
Tst ti«e
(•in): 720.00
Chrg ut
(Ib u«t): 23.30
run
tine
(•in)
0
60
120
180
24)
300
360
420
180
540
600
660
?20
vel dp
(M H20)
(in.H20)
0.05?
0.058
0.058
0.057
0.057
0.057
0.056
0.056
0.057
0.056
0.055
0.053
0.054
Units l^metric,
^English:
Y, DGM:
Pilot co:
Gas MM :
Pb (mm, in. Hg):
Tunnel area (*2,ft2):
Uood noist (.?. uet):
Burn
tunnel
te«p
(C,F)
78
84
90
90
87
81
94
90
82
79
90
93
91
DGM
rdg
(«3,
759.
789.
819.
850.
881.
912.
943.
974.
1005.
1037.
1068.
1099.
1130.
ft3)
103
100
500
100
100
200
200
400
800
100
500
600
823
DGM
temp
(C,F)
74
78
84
85
86
79
83
86
83
79
81
85
86
Samp vol
2 (s«3,scf)
1.009 266.506
0.99
28.56 Flou rate
21.78 (ds«3«,dscffi)
0.1963 149.47
11.39
rate (dry kg/hr): 0.78
UGH dH
CM
(in.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
0.670
0.
0.
0.
0.
0.
670
670
670
670
670
vel
(•/•in)
(ft/a in)
1127.51
1143.69
1149.98
1140.02
1136.91
1130.65
1134.08
1129.98
1131.70
1118.62
1119.84
1102.29
1110.62
PR
(2)
97.9
98.1
97.2
98.6
97.9
101.8
100.6
99.6
99.2
103.4
102.5
103.4
dDGH
vol std
(•3,ft3)
21.826
21.954
21.855
22.100
22.131
22.346
22.325
22.344
22.3%
22.634
22.335
22.259
85.49
17.640
460.00
1850.00
vs/Vals vs avo tunnel DGM
ave temp ave te*p
(C,F) (C.F)
0.01 1128.91 86.85 82.23
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv aanu:
Model no:
Lab name:
Tst date:
Run no :
Tst tine
(•in):
Chrg ut
(Ib uet):
run
tine
(•in)
0
60
120
180
240
300
360
420
480
540
600
660
720
SVEET HOME Units l=«etric,
flK-18 2=English:
ES/CB Y, DGM:
11-12-89 Pitot co:
B-l-4 Gas MM :
Pb (mm, in. Hg):
720.00 Tunnel area (*2,ft2):
Wood moist (?. uet):
21.00 Burn
vel dp
(*m H20)
(in.H20)
0.057
0.057
0.058
0.057
0.057
0.057
0.056
0.056
0.054
0.053
0.052
0.052
0.052
tunnel
temp
(C,F)
84
84
92
89
82
76
83
91
90
88
84
86
91
DGM
rdg
(«3.ft3)
131.837
162.100
193.300
224.300
255.200
286.500
317.700
348.600
380.000
411.400
442.100
473. 100
504.560
DGM
temp
(C.F)
75
78
83
86
85
81
79
83
82
83
81
81
84
Saop vol
2 (sm3,scf)
1.009 266.4%
0.99
28.56 Flou rate
21.70 (ds«3a,d5cf«)
0.1963 147.94
9.84
rate (dry ko/hr): 0.72
DGM dH
(m
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
670
670
670
vel
(m/ain)
(ft/min)
1135.87
1135.87
1154.19
1141.08
1133.78
1127.49
1124.83
1133.09
1111.66
1099.31
1084.91
1086.90
1091.87
PR
(2)
96.
100.
97.
%.
97.
99.
100.
100.
102.
100.
103.
105.
8
7
1
1
1
3
4
3
1
0
1
4
dOGM
vol std
(m3,ft3)
21.897
22.449
22.100
21.908
22.232
22.325
22.192
22.385
22.427
21.886
22.182
22.511
85.49
17.640
460.00
1850.00
vs/V«Ts vs ave tunnel DGM
ave temp ave teap
(C.F) (C.F)
0.01 1120.07 86.15 81.62
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manii StCET HOME units l=netric,
Model no: flK-18 2=English:
Lab naae: ES/CB Y, DGM:
1st date: 11-13-89 Pilot co:
Run no : B-l-5 6as MW :
Tst ti«e Pb (mil, in. Hg):
(•in): 720.00 Tunnel area (*2,ft2):
Chrg ut Uood moist (.?. uet):
(Ib uet):
run
ti«e
(•in)
0
60
120
180
240
300
360
420
480
540
600
660
720
16.20
vel
(M
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
055
057
056
055
056
057
055
056
055
054
0.054
0.
0.
054
055
tunnel
te^
(C,F)
90
82
84
75
87
86
82
80
79
91
87
88
88
OGH
rdg
(«3,ft3)
506.202
536.500
567.000
597.400
627.700
658.500
689.800
720.800
751.800
782.600
814.000
845.200
876.295
Burn
OGM
temp
(C,F)
73
78
81
79
81
85
84
83
82
82
84
83
85
2
1.009
0.99
28.56
21.64
0.1963
9.89
Samp vol
(s«3Bscf)
263.960
Flou rate
(dsm3a,dscf«)
148.08
rate (dry kg/hr):
OGtl dH
(IM
(in.
0.
H20)
H20)
670
0.670
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
670
670
670
vel
(•/•in)
(ft/«in)
1123.46
1135.35
1127.42
1108.03
1130.53
1139.54
1115.26
1123.27
1112.17
1114.21
1110.16
1111.17
1121.41
0.55
PR
(JO
99.1
98.1
96.3
100.3
99.3
98.7
99.7
99.0
101.7
102.7
102.3
102.0
dDGM
vol atd
(«3,ft3)
21.944
21.885
21.693
21.701
21.978
22.171
21.999
22.039
21.937
22.365
22. 141
22.107
85.49
17.640
460.00
1850.00
vs/VaTs vs ave tunnel DGM
ave temp ave tenp
(C,F) (C,F)
0.01 1120.92 84.54 81.54
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv nanu:
Model no:
Lab name:
Tst date:
Run no :
Tst time
(•in):
Chrg ut
(Ib wet):
run
tine
(•in)
0
60
120
180
240
300
360
420
480
540
600
660
720
SWEET HOME
fK-18
ES/CB
11-14-89
B-l-6
720.00
26.70
vel dp
(M H20)
(in.H20)
0.057
0.057
0.054
0.060
0.060
0.058
0.059
0.058
0.060
0.061
0.060
0.059
0.060
Units l-«etric,
2rEnglish:
V, DGM:
Pilot co:
Gas MM :
Pb (m«, in. Hg):
Tunnel area C«i2,ft2):
Mood moist (.?. uet):
Burn
tunnel
temp
(C,F)
71
84
92
87
88
78
76
87
92
91
86
90
85
DGM
rdg
(•3,
877.
907.
938.
970.
1000.
1031.
1062.
1093.
1125.
1156.
1187.
1219.
1250.
ft3)
213
TOO
500
000
900
800
800
700
100
400
800
000
062
DGM
temp
(C,F)
66
78
83
85
88
81
79
81
88
90
86
86
86
Samp vol
2 (sm3,scf)
1.009 263.949
0.99
28.56 Flou rate
21.53 (ds«3m,dscf«)
0.1963 152.06
11.68
rate (dry kg/hr): 0.89
DGM dH
(mo
(in.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
0.670
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
vel
(ft/a in)
(ft/nin)
1126.64
1140.35
1118.07
1173.19
1174.27
1143.95
1151.62
1153.48
1178.54
1187.25
1172.12
1166.56
1171.05
PR
C/.)
103.8
102.8
105.3
98.3
95.8
99.6
101.0
103.0
99.1
97.4
99.5
98.6
dOGM
vol std
(«3,ft3)
22.262
21.988
22.281
21.777
21.657
22.009
22.019
22.292
21.938
21.928
21.948
21.851
85.49
17.640
460.00
1850.00
vs/VitTs vs ave tunnel DGM
aw teitp ave tenp
(C.F) (C,F)
0.01 1158.24 85.15 82.85
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED //- 9 ~ U °\
DATE RETRIEVED // - I1-* - v 0
TEST LOCATION O"= •? 7>r/ /& .77*
SAMPLER SN 51 — '— ' ' — 2 iulF
•7 / . "7 * TORR ABSOLUTE Z., 3
POSTTEST B.P.T. /, (."T, (IN HG)
WEIGHT GAINS
PROBE 3 . °\
LINE
CONDENSATE S'<3 . ") .
FILTERS — /, Z.
FILTERJ2 — /e 4»
TOTAL (MG) £/* *%
•^
RUN# \J P-L ~ B~ I
- TEST TIME 12. l\ r 4MIM-. )
6
STOVE ID
WOOD SPECIES "^WoC-^
WOOD MOISTURE (Z DRY)
WOOD MOISTURE (Z WET)
WOOD CONSUMED (LB) A/&-5 (KG) £?.<.'
SAMPLE FLOW RATE PRETEST
TANK /•£>
?.<<<>
5>Vo
~~"~^6~6 TORR ABSOLUTE 7,70 .t
PRETEST LEAK CHECK
(—IN HG) TEMP. "2.7- (Q
POSTTEST
ROTAMETER C? 7 -(ML MIN)
START
-------
Page / of /
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY
RUN No. \)'PT- ft- I Placed in Dessicatoi-: Date/Time//-/^- &*) &O
STOVE MODEL No.
POSTEST
1
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
j — ,
//-/5/&yS
X*
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5 /)£•&>%'
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CALIBRATION WT.
WT AMOUNT =
PRE WT
* 5V-P /
c S0*3^
POST WT
a ^crv-cs
f $0-c*>
ROOM CONDITIONS
RELATIVE
HUMIDITY
/^£7
-2-/£7
BAROMTRC
PRESSURE
un
Initials
e
/»l*7?
t*c/t
OS
I
I
CO
(A)
(B)
-------
I
VO
CLIENT
PARTICULATE WEIGHTS SUMMARY Page. / of /
RUN No. \>Pt- ft" I Placed in Dessicator: Date/Time //-/£-S?
ES PROJECT P\ & 72-3 ' STOVE MODEL No.
POSTEST
/(, 7
Acetone Lot It
Acetone Sample Volume.
-.
. WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
i.
TARE WT
NET '
DATE/TIME
//-/6-<9V.VS5
x^
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7 7, '-522^
77.3Z23
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77* -2- ?/<£
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RELATIVE
HUMIDITY
2/ <^£7
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PRESSURE
£v /. 7
V.7.
Initiala
/
-------
I
w
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.CLIENT
ES PROJECT
EPA
A D
PARTICIPATE WEIGHTS SUMMARY Page L °^-
HUN No. - / Placed in Dessicator: Date/Time.
STOVE MODEL No. /)/<^/%'
POSTEST
Acetone Lot II ^ //
,
Acetone Sample Volume fa 2-
(BLANK CONG.) x
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(C)
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-------
CLIENT i
ES PROJECT J\D
PARTICIPATE WEIGHTS SUMMARY Page__/__of_J_
RUN No. ^6- -/?-/-/ Placed in Uessicator: Date/Tiine^2L£JL5J~L2Z
STOVE MODEL Ho.^k-ltf
POSTEST
*
' WT 1
WT 2
WT 3
WT .4
FINAL WT
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WT GAINED
DATE/TIME
/
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CALIBRATION WT.
WT AMOUNT =
PRE WT
. 5**o
• $V*%3
POST WT
« £000
• YW1
ROOM CONDITIONS
RELATIVE
HUMIDITY
?11<%*
T.6&&7
BAROMTRC
PRESSURE
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Initials
B
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/h&%
I
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I
(A)
.(B)
-------
CLIEHT
PARTICIPATE WEIGHTS SUMMARY Page / of '
RUN No. 5<£' B-/~^~ Placed in Dessicator: Date/Time //-/*'.
'22
ES PROJECT RO
STOVE MODEL No.
POSTEST
•
• WT 1
WT 2
NT 3
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FINAL WT
TARE WT
WT GAINED
DATE /TIME
//-// ®n c?0
//-//-'If*
//-3-s?
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.6*80*?
• *e>37
CALIBRATION WT.
WT AMOUNT =
PRE WT
* $o&o
• 5"e-<^?
POST WT
• So°°
• vm
ROOM CONDITIONS
RELATIVE
HUMIDITY
2 2-56^ V
T.C%7
BAROMTRC
PRESSURE
Z/-S ^
^/• ^.
Initials
D
^?^X?
r*\c#
I
Cb
I
(A) (B)
.)
-------
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Papa / of '_
RUN No. JTj^cJ^L/l^ Placed in Uessicator: Date/TiineJ/L/!_H_
STOVE MODEL No.
POSTEST
»
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
BATE/TIME
fl-12 &l*Ve
ll-ll &/IZO
(/-3-'«e\
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CALIBRATION WT.
WT AMOUNT =
PHE WT
• foffO
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• $cx>/
. 6*u/
ROOM CONDITIONS
RELATIVE
HUMIDITY
Z6<^7
7.Z@^7
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PRESSURE
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-LA 7
Initials
I
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<**
-------
CLIENT
ES PROJECT A/)/'2' 3
PARTICULATE WEIGHTS SUMMARY Page / of L
RUN No. S(j- /? V~7 piaced in Dessicator: Date/TimeJ/1^
STOVE MODEL No.
POSTEST
'
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
s~c~\
ll-tl^ t,067tJ
-<-7£/5
^7VS"
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.CG2-C/
CALIBRATION WT.
WT AMOUNT =
PRE WT
» ^"<3
ROOM CONDITIONS
RELATIVE
HUMIDITY
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•
BAROMTRC
PRESSURE
ZA 7
•zy. ^
Initials
t
/^^/f
/>i^<
td
I
(A)
.(B)
-------
PARTICIPATE WEIGHTS SUMMARY
Page
/ of
CLIENT _A'
ES PROJECT R D
RUN No.
Placed in Dessicator:
STOVE MODEL No
POSTEST
. H K^ * 0
'
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
//-//- *H
(&. ; T^
-------
CLIENT
ES PROJECT R 0 -II 1
PARTICULATE WEIGHTS SUMMARY Page / of /
RUN No. /?-/- £ Placed in Dessiqator: Pat e/T line //-/
STOVE MODEL No. /?A*
POSTEST
;
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
//-/<3 & WO
Ihlt e /Z^^
ll-l>~?>Ci
FRONT
PTr.TRR 1!
/9£-/*s
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CALIBRATION ,WT.
WT AMOUNT -
PRE WT
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POST WT
• ^OTjO
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ROOM CONDITIONS
RELATIVE
HUMIDITY
2o^65
2,/<9^-7
BAROMTRC
PRESSURE
z/< •?
•Z/-7
Initials
t
/*ic4
s^r^
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
EPA- Run I • •
ES. Project I
Wood Heater Model
Operators
AK-IS
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) "Thermostat Setting
Primary Air Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
•z-t, a
!T«?
1?
^
/Co - /O, O
i.CO-J
Post Test
•z./,S" •
6
-------
ENGINEERING-SCIENCE, INC.
Client /f//"un '
WOOD IICATEK CERTIFICATION TEST
TEMPEUATUKE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page / of
Date //- "9 - ft ct Hood Heater Model f\^~(S> Coal Oed
ES Projec, f
M
1
1
1
1 — »
OO
'1me
Sampling/
Clock
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Catalyst Tenp
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Surface Temp,
lop
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Tun.
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Temp.
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ftf_l
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater A /< - / X
Date ) i . ty ~ & •%
//)<• // T,<
l^f> II So
/I*) I7.A*>
1 C,Q ii.2£>
iL^i n 15
I %& /"I *>f>
t Cl5 /3<^
1 10 Il2o
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2 T5" 1*6 S"
Z ~?S} /4l&
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25,3
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1.00. I
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Head
( PS), in.
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tf & 5" v
O'fi-Zt'
^cj «5"r
- c^ 5~C
* o5" T,
. o^o_
Orifice P
Djffere
( H), In.
Desired
0 • (j 7
r> * te 1
S) , £,->
/> / /, *?
1
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ntial
H?0
Actual
/J - Itl
&,(,-)
f) , (f~)
A. 6,')
*6 1
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^ ^7 /
^ v' ^
* ft 7
p /;, "7
.6-7
. 67
(fc>7
i 6? "7
.1*7
,k>7
(cT
TEMPERATURES
Dilution
Tunnel
* 67
* 67
Meter
In
^> Tf
^ •?
•? y
*£*>
•f,"^
^^g.
^ Z-
*? 2_-
<&0
Meter
Out
-C7
/i C7
69
5^-7
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Pump
Vacuum
1n. Hg
7_
•2—
7^
Z.
2.
z_
^
Flue Draft
in. H20
-------
I
tu
I
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I
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o
SAMPLING DATA (cont.)
Hood Heater /)J<
ENGINEERING-SCIENCE, INC.
Date //- 9- ^"1
.^~)
Sampling Locatio'n Ov*.//^ r/ &,FPe. / "~)
Sample Type 5"jCi
\. Clock Time
Sampl1ng\(24-hr
time, m1n\Clock)
~^2Z5 L5£&_
^75" • l&£>*>
39£> )6>2£,
y&5 1^$
V2o Ib*^
V3J_$o' l~?2o
y&5 I 7 ? 5
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^? /£> j% 1c
Sl^ /<,^
"jVc /6<^
6" "i^T /'^'T
^ 7^ /V^>
^s-
6 7f :£//f O
-\^-/:>/. *>y
^ f
, o 5c>
»(<->/
j/5 y
t(i'5V
.- ofry
Run Nu
Operat
Ori f ice Pressure
Differential
Desired
i
Actual
a/p 7
^ /»~7
^67
x<<, "7
* 4,-)
t t> 7
, <^,7
/ /, 7
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t L- 1
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, (, -7
, <;, '7
•C7
' 6 "7
A "1
,6 "7
"^
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o r y/r « /^ A:J //
TEMPERATURES
Di lution
Tunnel
•leter
In
% 7
^.q
S 2
^y
S^
-
Meter
Out
S-5"
ViV
S/
ft /
^ y
Filter
7*?
"~7 ^/
iy
~?(s
Impinger
/7 £
^T '^
5"3
^ z
•
.
^z
'ump
Vacuum
in. Hg
•z.
••j
?
•2-
7_
Flue Draft
in. H20
7/
-------
FUEL MEASUREMENTS
Date //-'
Project No._
Run No. -R-l —
Mood Heater Manufacturer
Hootf Heater Model Ak
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
Fuel Piece Length_
4x4
~ Actual Load Weight
Moisture Meter Calibration A2S—
U/«.cc/ r*~a.°F
Piece No.
2
3
4
5
g
10
11
12
13
14
15
16
17
18
19
20
Moisture Content- (Meter - Dry Basis)- CoivceTcd.
Readings Average
n.o
/AJ
Zf.g 11.Q
ILL \RJ
Overall .Fuel Moisture Average
I-B-l-21
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
fef/V Run t "U' - \ -
ES Project t
'Wood Heater Model
Operators
p\C'\
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (i)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
2.1. ft1^
<£ *>
11
a
(4iO//o,O
WIV-
Post Test
7, /. •* ,£> •
^5-^ "7^7
/
-------
WOOD IIEATEIl CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
'ENGINEERING-SCIENCE, INC.
Client ^ />/9 Hun I
/3-x-z
Test Fuel Charge
Page / of /
Date //-/^-21 Wood Heater Model /) k~ /<£ Coal Bed
ES Projec, f
c
M
1
Cb
1
i— •
1
Time
Sampling/
Clock
£> ^Ifrft
CJQfi
j3 ^gp
Jin GBf9
fro hrp&^
//o6>
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/3c^j
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/50O
; <£oO
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:uel
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Pr.
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nternal
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7^y
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7Z
70
~ "ft
-------
K>
R ui_j ULuL>|
P, ,-jt.j ij. j-rJ
ENGINEERING-SCIENCE, INC. SAMPLING DATA
Wood Heater /)/<-/*% Start Time
Date
//, /O - *&*)
Samp ing Location O*/-si7W/ ^-777-
Sample Type <^
Run
Stop Time
Probe Length and
g-/-z
Type /v "' &/*>??
~ J
s ) /&4 /=• 7^> /?
5<^
.Assumed Moisture
*/*?<:>
Sample Box Number /5
Meter Box Number
Meter H
f^^
flJ* 7er k /?
Pretest Leak Rate 4f <*¥/<}"
Post Test Leak Rate »or>/ c$* G> f*
hjpiaJi /'"^«Aa Read and Record All Data Every Minutes
gJLu^Ji U^u^j
uuuj '-^lock f1,ne
S cftfplQ Hyi E^i4fc^?-S C
time.mln Clock)
Wooc
(7 <9^ / o A"?5 '
Cjo leQ&n
10*2- /O*3$.Q.
I'LO //y^t
/ 3$^ // W($t<
/ 5^ // 30
/OS //V5"
/ l*)0f>
1_cj^ ll,/^
7-7<> /9^<>
1 tt ItrY*)
~*>ao 1V&O
•W? /V/-?"
\— -^%^ /JCtf<-
leading
'i»Jit^f^;3«55
1nq Locflt
fe Type -
umber y^
tw/^» ^
nt Temper
etrlg Prc
c P/essur
r f/frilfeoH
/f Cr^-* '
/J -1 3-s ^
O
/2 <••> ^^u
ttir^ 5"^V?j
i S ^X"P> T ^* "
a f p -^i /
)_jjffj^ &
• * o 57
a c' 5e*^
0 £T^S
'^Cfli?^.
/ o 56
f.o'yj
*f>£\ -?
o£ 6>
j @ *5~J
a (f?
.066-
.o'SB
-<96>(
Orifice ]
Differe
( H), in.
Desired
ret' $L • .
f-/
y
/, ?;<;
7^ /:5
A rid Ri'C.f
i ' ' ; • '. i.
ressure
ntial SA
H?0
Actual
.. 6> 7
T*«rf>"?
j <^ 7
e (0 7
e&~7
.67
,07
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.^l
- .f>4>f •> i ! — . <,— 7
1f'L il-IO DATA TEMPERATURES
Di lution
Tunnel
,:it.! Ever)
Meter
-7 ^>CG
fro
-j tjl'i i
Ass
^^•bon
Mi?t
lie i
e u>n«j
o^ -^ui^
umco no
()l^ IdOX
er IJQX
er II
Iff^lp LC
I: U:SC
Hi nu te;
?
flJl* P fC J
J^l^L-.
al^^a c e
^-iS*)(
Lean Kate too/
SV .C2
82_ • 5"1?
7-9 ^<5
1 ^
Pump
Vacuum
^-ijuJig-
-J2___
' ^r- X/5
/^J{_
7^
i /?
*"I-V ft?
c^p**1 v*
,._2
'2—
'2_
t «-
Flue Draft
--in. H20
^,1^
-^J1
-- ,
.
-
. .;,..,.,,. ,j. . — - *.-
-------
I
N>
IS 131
Ol\
ENGINEERING-SCIENpE, INC.
Hood Heater AIO/8
Date
//- IQ ~¥fi
Sampling Locati
Sample Type
on ~7 5 /^jf
J31P V5-V.
/5V J6,3/5
*5/<3 /93/j
525 y^V$"
4?Vo y«^o
55*T i*i/5
f;7O / ft 3o
5"2>5" /l^*?
bert lO
(, 1^ /9 /» C»
/a6*y. £,
6^-^
72-). /
Velocity
Head
UPS) In.
»O(bO
to5"£i
»G5-isi
,os* ft
,05" 'rS
^^ ^ -^
^ •*> ^
fo£>c)
A o*?9
a f~7
tG '7
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^ OP /
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f6>~7
* (,7
.(, 7
67
r(,1
* (s 7
* ff 7
tic~t
• fj> 7
• ^°~~1
TEMPERATURES
Dilution
Tunnel
Meter
In
Qf.
S*5
8*6-
•r? C-
& 7
-
Meter
Out
$- V
^v
V?
^*5"
-------
FUEL MEASUREMENTS
1/8 !*«• /iy. /l3_/±<«
6 111. ^6_ili7
7 9,5 9,? _/o.-2
8
9
10
11
12
13
14 .
15 .
16 ___
17
18 :
19
20
II.T
I-B-1-26
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client '£ PA
Run t
Date //-//-
ES Project f
'Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) >l8Q Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
Post Test
/. 7-5
7 2.
/V
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2CK Dry /!>&'
Fuel: Dry Kg
to
Wet U3°\
C\1
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Velocity Traverse
Temp
.
Ave.
Pitot Leak Check
Static
I-B-1-27
-------
WOOD IIEATEIt CEUTlRC/VnON TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCSENCE, INC.
Client l~P/JHun I /5 ~ / " 3
Test Fuel Charge
« -J
Page
Date l/-//-^*] Wood Heater Model /)/<-/%' Coal Oed
ES Projec. I
M
1
1
l — '
1
ro
oo
Time
Sampl ing/
Clock
to/0
to 31
/a V /
'// / c?
I'l JO
f3! lO
//// ' f}
f^f ft
/(//{>
n /o
/ft /o
/9/a
2.0 1C
1-1(0
T.T./O
L
Test
:uel
Ibs)
V- y
/v/0
JI.'L
9/ £
"-j/t.
£feCj
~2e>;~L
/&• 7
S.o
/V' 3
^3» a
6. 1
0 ~^
9, a
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(In
i»
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,&19
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9/1
6.7 'Z-
S^ii-
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T5"^
77^
JJ*>C
/&ZY
b6V
J £^£j
//Q *%
75-5
5 ifj
\j£ ~y
ni
97?
7$£
ftUC- Surface Temp.
Top
7_£^
"?2i
?v^
i/y
7V
?5j
2/-J
^9<^
32-t
35^
3^?
Hear
Uottoui
Right
Left
Stack
Temp .
7V9
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•^y/
~3 ?^
27^
•2^"2-
35
/y £/
T^>y ^/
"7»-> "T?
TZ^
Oil.
Tun.
Temp .
•7 ^
w
OO
9<5
S7
<£<$>
7Z-
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater
Date /V-/7^
Sampling Locafion ^
Sample Type
Run Number
Start Time
Stop Time
A-/- 3
Ope rato r jy\ erf /d//
Ambient Temperature •?&
Barometric 'Pressure •
Static Pressure, (PjJ
Filter Number(s)
Meter
/. ff /
Probe Length and Type_
Pi tot Tube Coeff1cient_
Assumed Moisture //
Sample Box Number ^
Meter Box Number
Meter H
55-
Pretest Leak Rate a&z>
Post Test Leak Rate t
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
£? £ofa
)5 /><"
"3*9 '/o
VT zz
6>o n fo
*?& ^6
)o^ 55
i2o f). /o
11$ 2C
tSO V6
!&>*> C.C,
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-l/o HO
Z2£ $4
2V<3 ^V /<7
75-5- -2^
I'M} LJO
2.f> *>*>
1t>0 /*i /*>
VT 2?
^-^, t^o
^VC ^^
3^ /^ 10
Gas Meter
Reading.
(VJ ft3
789«/
^tQ* *>
.
^V
&
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a 0^7
t O ^")
.057
. < , 5' ")
,0^-~)
* <3 f> 7 '
„ 0-5-7
^ OC7
»-o S 7
OC1
& $ *) &
Orifice 1
Djffere
( H), in.
Desired
ressure
ntial
H?0
Actual
tb~l
t£c>~)
i b'7
./*~>
» ff,~l
,(„—,
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.07
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, 61
.^7
.67
« 6 7
.^X
* /£"?
„ ^7
. (^ 7
*£,7
. <>7
TEMPERATURES
Di lution
Tunnel
Meter
In
7 5"
•zC ^
^
-------
ENGINEERING-SCIENCBE, INC.
SAMPLING DATA (cont.)
Hood Heater /?/<
a
Date
Sampling Location
Sample Type
Run Number_
Operator //
Clock Time
SampHng\(24-hr
time, min^vClock)
Gas Mater
^eadi nq
Veloci ty
Head
(&PS) in.
H?0
.05 S
)ri fice Pressure
Di fferential
. ll;>0
Desi red
Actual
.6"?
TEMPERATURES
)i lut ion
Tunnel
leter
In
Meter
Out
Filter
Impinger
'ump
Vacuum
n. Hg
Flue Draft
n. H?0
7V, y
.- (.'I
$.&.
J3L
^ri 7
79
.05^
rf/
71
055
.67
I
w
I
I—»
I
1-0
O
(,l,o 11 /<
- (2
"3L
-------
FUEL MEASUREMENTS
Date U-U-S?
Rb r
Project No.
Run No.
Wood Heater Manufacturer _
Wood" Heater Model
^-/ R
Circle One: Pretest Fuel •
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
am
ES Project i
'Hood Heater Model Ak -1 8
Operators U^ , A Kr £
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr) i"1(ll
Primary -Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (CF)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
•2.1.1 <*
f»~?
/y
&
/b>ci/l£>,Q
WA
Post Test
2. /. t,
-------
\
TO
I
I—•
I
OJ
WOOD IIEATEH CERTIFICATION TEST
TEMPEUATUHE AND FUEL CONSUMPTION DATA SHEET
'ENGINEERING-SCIENCE, INC. 0
Client .£ Pfl Hun I /5-/~
Date /A/Z -
Test Fuel Charge
"2.1.0
Page r_ of
ES Projec. I /Z. 3 Operators
Heater Model x/A'V.^ Coal
itors /^X? /^J /V
J f> ,• o^ '
5/£ '//jy*
3?y
'ZsY
)•*$-)
2,27
32 y
1?"7
s.y^
•^•f?
•5^ 5"
337
D11.
Tun .
Temp .
•sv
firl
?y
vf
1C/
£<2_
~7 (a
S3
9 y
9 o
ffc-/
S&>
*?/
Room.
Temp.
d»7
^S"
x8^ £l
7V
px
^ ^/
/ O
?/
•y-y
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date //. /-z
SAMPLING DATA
Sampling Location
Sample Type ~
Run Number
Ope rato r
y?L
Start Time
Stop Time
lb&6
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter /'^0o ~$fj
v< y^"
(sG llrt>
7t K
<3o in
/O^ t/ * "7 fo
1^ ) c,
1 To to
/A*) L/9
/ $0 ]~*>el-,
/9< /<
2 /o ^>
?
r> ^^ cy<^
~?£>r5 / «7 <:.<;'
\^^ £r-
^— •— ^—*"-"" „ ._ _ . /* fe>*-rri> ~
Gas Meter
Readl ng
(vm) ft3
/<£ ?/ /
/ "-j '"> "S
.
2 2 y. -*>
i*2 C~ ^ ' J
"2-*S<6 *^"
— * ' — — - — .
Velocity
Head
( PS). in.
H?0
,0^1
of TV
, (;*><-!>
A <-> ")">
j C' 5" 7
<3 •"> 7
, 6 S'7
,O56
^c1^ $
L<-' Cl~l
., 65"f\
,05-7
t o ^ 7
. £' ? 7
u. C' T^>
o 57
j a ^'7
a& c, 7
„ o
• 6 '7
/6V
.6 '•)
. 6-7
.67
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- 6 /
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* /
^q
Filter
6} 9
Impinger
^ V
72. ^/
72-
$•/
77 5'^,
7 S^ 5~<£
7 7 • 5<^.
72
5" "J
7 .-? 5 ^
Pump
Vacuum
1n . Hg
•p
Z,
2^
-»
"2_
7.
-j_
^
Flue Draft
1n. H20
I
td
I
i—•
I
LO
-------
I
tu
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I
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S^^ •
j/\
ENGINEERING-SCIENCE, INC.
•ir L i nu u
Wood II
Date _,
f\ 1 1\ \Lunu . ;
eater X? A - / ^
//-/Z- ^^
A^ 1 (
Sampling Location Cwf&^rS Ai-Vie
Sample Type <^~<
r^~i
Run Number /?- v — V
Operator /h~c /% it) Si*
'• "X. Clock Time
Sampl1ng\|24-hr
time, mln x^lock)
^C~o~ Kts&_
-575" • I
J^35" ^c±
"?<0
4"T
/ 5'~?~
•7~V0 )c)c}n
^T'T'T / 3o
r vc
/£/*>" /*?
^> 3c» ~?e
{py-i Vc
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7 c1^" v ^"<^
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A & ^ O^
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i <> 5"^
.,06 ^
• asr5
i OS1-/
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. 6 S "-/
i ^5 'S
, ^5'C_
. c 5 "^
_ 0 ^2
o c» 5"2
»<7^7-
. o 5" L
Cf^i L
«? 5Z
)ri fice Pressure
Oi f ferential
(AM), -in. ll?0
Desi red
6> 7
Actual
*
.G7
.67
•<^ "7
•07
• 0-7
/x "7
. 67
/ 67
. 6? 7
.6 7
.^ -7
TEMPERATURES
)i lution
Tunnel
1eter
In
S'4?
S 2
* 7
fr '^
S'V
'
Meter
Out
ft 3
V-L
ti'TS
^ /
<%/
Filter
75*'
7V
•7^
7 V
7#^
Impinger
•5" V
5~c»
IV 3
^7
•
5"?-
Pump
Vacuum
in. Hg
Z
0-
"2_
7
•2L
Flue Draft
1n. H?0
-------
FUEL MEASUREMENTS
Date 11
Project No. ^
Run No. "R _ | _
Wood Heater Manufacturer
Wocxf Heater Model
A \f_- l
H-
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
Fuel Piece Length_
4x4
Test Fuel
1x4
Actual Load Weight
Moisture Meter Calibration
W«,ca/ T*~,p. °F
Piece No.
I &<>*
2
3
7
8
9
10
II
12
13
14
15
16
17
18
19
20
Moisture Content- (Meter - Dry Basis)-
Readings Average
9-3 i{,8 li.'Z-
rz.
rL&
Overall Fuel Moisture Average
I-B-1-36
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client £ ft) Run / ft- /- 5
Date //- /"3 - g «7
ES Project f R & - ) 2
"Wood Heater Model Ak.--( R
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) _ Secondary Air Setting
Achieved Burn Rate (Kg/hr } ___ . 'SS't- Thermostat Setting
Other Settings
Primary Air Setting
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°FJ
Relative Humidity (>}
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
Z./.6.-7
/<,*!
)1~
o
/£.°r
Post Test
I./. &/ •
-> I
1.^
CJ
la..c //n .f>
/
\ V ^ VX
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
to
Actual Fuel Charge Wt. l(o, Z.
Fuel H2K Dry /C.^l Wet
Fuel: Dry Kg 6,6 Z '
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Velocity Traverse
p Temp
A 1 B 1
2 2
3 3
4 4
Ave.
Pi tot Leak Check
Static
I-B-1-37
-------
TV-l-S
WOOD IIEATEH CEIITIFICAT10N TEST
TEMPEHATUUE ANU FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
CHent t: Pf) Uun I
K-i- 5"
Test Fuel Charge
Page / of J_
Date //-/"3-^? Wood Heater Model ^7 /<-/"? Coal Bed
E5 Projec. f
M
1
CO
^^
l*>
OO
Time
Sampl ing/
Clock
G^SO/^
rf%t>
| &6O
\66
140
1?^
tV0Ts
XS^TS
/^ "ft
n#i,
iKsv
/9<^,
7£> £K^
Test
Fuel
Ht.
(]b«)
V.ft
A»,d
T4?
6-0
?r.^
5.Y
•9,^
V^
y*7
?*/
•c,-^
"7. '3
b.O
Flue
Draft
(In
H?0)
v "-&K.A
/$?? ^,t>/K.i - -3.1 •&
s
Catalyst Temp
I'rii Hnternal
3I±/.
^X>
At
7<'-
TV ^
24 Cp
•iT,T
7./T
/97
/§-/
-•xiT
•?s^
2^ C-
274-
Right
Left
/Vg-
Stack
Temp.
:v/v
^«2f
-i-'il
£<^
2-as
/751
/4Z
irv* f1
/7V>
/36
Z,
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number_"
Operator
Start Time
Stop Time_
Probe Length and lype ,/t/ -
Pi tot Tube Coefficient a 7^
Assumed Moisture *•/
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter if-- T
Sample Box Number /?
Meter Box Number ylX-FVc
Meter H /ts#
Pretest Leak Rate_
Post Test Leak Rate rf
ILS '-/S
/9-T If
~2l6 1,0
2Z*T tyf
2V/j > a l^av
1/f It '
-^10 y0
5T~?
,05'Q
, GSS
,(3^ (i
, t-'SS
. .Cs1nf>"
.OSV
. 055
,05^
f ^ (i
.r>5^".5
r657
, a $C>
j 0^1
« f-> S'S
j O i i
, 0S S
Orifice 1
Differe
( H), in
Desired
• ^7
ressure
sntial
H?0
Actual
.67
.6-7
• if~l
.<,-)
,<*7
.(*-,
Q"7
•G '?
<6- 7
• /
c?<5 V &
7C'- *? "^
?,<-> ^ ~s
73
5"f
Pump
Vacuum
in. Hg
"X
-^
~2_
<
'7
^
z.
Flue Draft
in. H20
I
U)
VJO
-------
SAMPLING DATA (conI.)
Wood Healer /)K
I
H-•
i
4>
O
ENGINEERING-SCIENCE, INC.
Date /A /"?-£-?
Sampling Location O-f4J^ /<5
Vf ^ / *>
£j/£> rV>
^"^^ V?
5V^> / ^J f>f>
tt*? 1 1
£>
5"$^ V^
^
/ tj* ^~j£
/ i./) i Q ffify
&~?5 )$
b°to ~$o
7^5" y^
Gas Hater
Reading
9 "?^-tf
"9 57' ^
732.^
^-/y, o
<^y$"x 7,
Velocity
Head
(APS) in.
* c> -$"7
.o6>
. #f C
4 ^> 5(-
a'oc.; %
• 05Y
fj £<^
C CX
«C'5^
f~\ "T? LJ
v *-' *i 7
/• O 5V
.<, 5 y
.o5V
• &'>'>
< o 55"
o c> 5V
^ £> ^ ^
d 5" ^"
* o Tf
Dri f ice Pressure
Differential
(All). -in. II20
Uesi red
Actual
^ £ 7
'C-7
'C- O
» ^/ 7
v<^ 7
• (s 7
,^,-9
/67
• ^ "7
, 67
" /
* 6 7
TEMPERATURES
Ji lution
Tunnel
i
deter
In
ft 5~
^"^/
?5
^y
^ s
-
Meter
Out
?' 1
•5? "2-
S' 2.
2"7
g1 3
Filter
77
76
7V
7
-------
•&-/-S
FUEL MEASUREMENTS
Date \\-\'^-O0f Hood Heater Manufacturer
Project No. £^ \ 2x"*» Hoo
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f '"K , |
ES Project f
"Wood Heater Model r\K- ( P,
Operators -S |A( fc . V/^ "A bl
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (*F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest | Post Test
?.<•'$<-/
6*
i 9.
0
16 0 110. 0
MA
-^<-S"-5_.
tS&y
/<-/
£?
fojy/j43.. C>
\
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2di Dry
Fuel: Dry Kg
to
Wet
LOADING/TEST START OPERATIONS
By-pass _ _ Air Settings
Door _ Comments
Veloci ty Traverse
Temp
A 1
2
3
4
B 1
2
3
Ave.
Pitot Leak Check
Static
I-B-1-42
-------
ENGINEERING-SCIENCE, INC.
Client (=^rfl~ Hun I
Date
ES Projec. I
WOOD IIEATEH CEUTIFICAT10N TEST
TEMPEUATUHE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ued
Wood Heater Model
Operators
Page
Time
Sampling/
Clock
/Sbo
{6>&t)
I
td
I
K-
I
4>
OJ
Test
Fuel
Ht.
(Ibs)
100
/7,5
/y,
IL*
Flue
Draft
(In
H?0)
0,027
Comments
ttt
n/->
771
Catalyst Temp
n-
nternal
•yz-v
Post
("ZV"
5V9
ZIL
Top
Surface Temp.
Kear
Uottom
3 V
170
31-7
3?-?
Right
Left
Stack
Temp .
271
Oil.
Tun.
Temp .
7C-
Room.
Temp.
70
7?'
7?
7
~7
7V
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type =
Run Number
Operator
&cl
Start Time
Stop Time
1
Probe Length and Type yy v
lAWV
Ambient Temperature
Barometric Pressure
Static Pressure, (P^Y
Filter Number(s) ]
Meter l.oo^
Pi tot Tube Coefficient ,^r^7
Assumed Moisture i~f
Sample Uox Number
Mater Box Number AV We /i
Meter II
Pretest Leak Rate £j_,
Post Test Leak Rate 0
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
tlme.mln Clock)
£) £> "7 £><->
1^
3<=>
i/<^
/ r, 6 £3^
fO
/^ J
1 7O O*-r & '-•'
/VS
iSo
'/So /o*0
tc("5
Z/b
1,75
2.Vo C do
21 o
"2-85
I'V.D (~ICC>
3,5
Gas Meter
Readi ng
R>7 7, Z-H
9O7. 7
•^-30 . ^
cl'7o. o
C'^0 ,cj
//j -Z,/ M ef
Velocity
Head
( Ps).1n-
0,()S7
i ^S'Ti
/ &S7
. ^>5^
.05-7
. t) 'bt-/
t<$5^(
.o1? •-(
• o^v
.,05-7
,d6? O
&e&
,OXi 1
O^ci
,oGc>
OCcO
tod>o
. &&e,
«^^T8^
, 059
^ o -sr^
Orifice 1
Differe
( H), 1n
Desired
• fc-7
ressure
ntial
H?0
Actual
^ ~7
. C^~7
.67
k "7
6^
,<»~7
.(?—?
o (C> /
' V5 i
^•7
<^» 7
,67
.4-7
.6 ?
. C 7
.6 7
' v> 7
$ fc> /
,^, 7
.-{, 7
, ^,7
^ ~7
8 z
r^> <.-
O^r1
70
_
c".
•£ ,
Z.
^—
Flue Draft
1n. H20
-------
SAMPLING DATA (cont.)
Hood Healer
B-'-t,
ENGINEERING-SCIENCE, INC.
Date //-/y- S^
Sampli
Sample
*• 6 O
ng Location CVcsJ/iLc/ fit-Wt
Type ^" • /T
-T,CIG i&
V/3 ^~ V^
<-/3c? /v<=t>
v? f / 5
L/
^f^r ^^r
5"yo "jo
*? Z<7 V5
^
56*7 V5"
&aO /7&*>
(ol^ I *>
^3o 3o
l^uc y<"
^^r, /% 4Q
foTi i S
MO In
Gas Meter
Readi ng
//">9 ?, ')
// '2 ^"v /
//5V&. 4/
I/O "7 G'
// o /« •}
/2/9 ^o
17 ^fl OtT-
Veloci ty
Mead
UPS) in-
M70
• o5-f
<"j<^f>
-«i>5'7
•• c> S S^
a O 0
. <56 /
^. tf & CJ
'cCc ^
. £60
« O&> /
, C)&>/
04 /
* 0(0 £>
0 C' <^' 0
, ^> <^ y
, £$ tj
,V5>'1
,06.0
,*6 I
C6 C
Oril
Dif
Ues
Mce Pressure
cerential
red
• <5 7
12.0 /ci , <*&O
Actual
4<^7
-(•>"}
-6~?
'£• ~?
» "9
'67
i^~7
, ^^
, ^c -7
>(r^7
* 9
« ^ "3
, & -j
' <*• P
* /r, 7
. Cf '"7
167
THz"
-
TEMPERATURES
Dilution
Tunnel
Meter
In
^"T
^?/ — •
c?/
9/
37
^"»
-
Muter
Out
By
- ^fl -
%%-
9 '&
^6
^
-------
FUEL MEASUREMENTS
Date rUm^S^l Hood Heater Manufacturer
_ _
Project No. •fi't-si Wood" Heater Model t\ k - (
Run No. -ft. i -Q»
Circle One: Pretest Fuel • Cjgt
Fuel Type and Amount 2x4 _ 4x4 _ 1x4
Ideal Load Weight _ ; _ Actual Load Weight
Fuel Piece Length _ _ . _
Moisture Meter Calibration 121
*/«•
-------
TEST SERIES
B-2
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Kate, and Sample Volume Calculations
I
to
I
N>
I
Stv manu: SWEET HOME
Model no: flK-18
Lab name: ES/CB
1st date: 11-15-89
Run no : B-2-1
Tst time
(mm): 600.00
Chrg ut
(Ib uet): 25. 40
run
time
(mm)
0
60
120
180
240
300
360
420
480
540
600
vel dp
(mm H20)
(in.H20)
0.054
0.055
0.055
0.056
0.055
0.055
0.054
0.053
0.053
0.051
0.051
Units 1-metric,
2=English:
Y, OGM:
Pilot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Mood moist (.'/. uet):
Burn
tunnel
temp
(C,F)
62
81
91
8?
85
87
86
82
84
90
98
DGM
rdg
(m3,ft3)
313.925
343.800
374.500
405.200
435.900
468.400
497. 300
527.900
558.500
589.200
620.555
DGM
temp
(C,F)
61
71
77
79
79
80
82
82
82
83
86
Samp vol
2 (smS.scf)
1.009 221.366
0.99
28.56 Flou rate
21.76 (d5m3m,dscfa)
0.1963 148.33
11.21
rate (dry kg/hr): 1.02
DGM ell
(mm 1120)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.671]
0.670
vel
PR
(m/min)
(ft/B
1081.
1111.
1121.
1127.
1115.
111?.
1106.
1091.
1093.
1078.
1086.
lin)
62
28
50
54
38
42
21
89
91
97
79
(52)
103.
103.
100.
99.
106.
94.
99.
101.
102.
107.
1
1
3
0
3
0
5
1
4
4
dDGM
vol std
(m3,ft3)
22.254
22.438
22. 187
22. 105
23.401
20.770
21.911
21.911
21.982
22.410
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1102.96 77.75 78.36
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
DO
I
to
I
NJ
Stv nanu: SWEET HOME
Model no: flK-18
Lab name: ES/CB
Tst date: 11-16-89
Run no : B-2-2
Tst time
(oin): 840.00
Chrg ut
(Ib uet): 33.40
run
time
(nin)
0
60
120
180
240
300
360
420
480
540
600
660
720
780
840
Units 1-metric,
Y, OGM:
Pitot co:
Gas MU :
Pb (mm, in. Hg):
Stack area U2,ft2):
Wood moist (?. uet):
Burn
vel dp tunnel
(mm H20) temp
(in.H20) (C.F)
0.056
0.056
0.056
0.055
0.057
0.057
0.055
0.055
0.056
0.055
0.056
0.056
0.056
0.056
0.054
74
86
95
%
92
89
89
94
93
88
90
87
84
83
82
OGM
rdg
(m3,ft3)
622.
651.
682.
713.
744.
776.
807.
839.
870.
902.
933.
965.
996.
1027.
1059.
307
800
600
500
700
400
300
000
600
100
600
200
700
900
195
OGM
temp
(C,F)
73
80
85
85
84
83
82
85
89
88
86
86
84
83
83
Samp vol
2 (sm3,scf)
1.009 310.709
0.99
28.56 Flou rate
21.68 (dsm3m,dscfm)
0.1963 148.30
11.63
rate (dry kg/hr): 0.96
DGM dl
(ma H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(ft/min)
1115.
1128.
1137.
1128.
1 1 44.
1141.
1121.
1126.
1135.
1120.
1132.
1129.
1126.
1125.
1104.
98
45
72
53
72
61
40
49
66
38
58
49
38
35
05
PR
97.
100.
99.
100.
100.
98.
103.
102.
99.
101.
100.
99.
99.
9).
1
6
4
4
2
1
6
1
3
2
2
6
1
5
85.49
17.640
460.00
1850.00
dOGM
vol std vs/VmTs vs ave tunnel OGH
(m3,ft3) ave temp ave temp
(C,F) (C,F)
21.401 0.01 1127.92 88.13 83.73
22.059
21.928
22.141
22.537
22.009
22.620
22.425
22.191
22.231
22. 384
22.313
22.181
22.290
-------
Method 56 Proportionality Rate, Floo Rate,
Burn Rate, and Sample Volume Calculations
I
N>
Stv manu: SWEET HOME
Model no: flK-18
Lab name: ES/CB
1st date: 11-17-89
Run no : B-2-3
Tst tine
(•in): 810.00
Chrg ut
(Ibuet): 12.60
run
time
(mm)
0
60
120
1 80
210
300
360
120
180
510
600
660
720
780
810
vel dp
(mm H20)
(in.H20)
0.055
0.055
0.053
0.051
0.055
0.055
0.050
0.05 1
0.051
0.053
0.052
0.052
0.050
0.050
0.051
Units l=metric,
2-English:
V, DGM:
Pi tot co:
Gas NU :
Pb (mm, in. Kg):
Stack area (m2,ft2):
Hood moist « uet):
Burn
tunnel
temp
(C,F)
72
89
98
98
97
71
75
90
83
83
86
91
96
93
91
OGM
rdg
(m3,
60.
90.
121.
152.
181.
2I5.
216.
277.
308.
310.
37I.
102.
133.
161.
196.
ft3)
507
100
300
700
200
900
900
600
700
000
300
300
500
600
711
DGM
temp
(C.F)
70
77
87
92
89
77
65
73
80
79
79
81
81
81
81
Samp vol
2 (sm3,scf)
1.009 312.106
0.99
28.56 Flou rate
21.66 (dsm3m,dscfm)
0.1963 113.82
16.81
rate (dry kg/hr): I. 15
DGM dH
(am
(in.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
0.670
0.
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/min)f
1101.11
1121.92
1110.32
1120.75
1130.06
1106.18
1055.98
1081.33
1071.13
1095.30
1087.91
1095.85
1076.50
1073.60
1082.32
PR
00
97.0
99.0
99.8
98.1
91.1
96.5
105.3
IQI.3
10I.3
lOO.I
10I.3
101.2
102.2
101.8
dOGM
vol std
(«3, f t3)
21.791
22.231
22. I8l
22.050
22. 31 1
22.306
22.595
22.516
22.397
22.138
22.223
22.281
22.232
22.815
85.19
17.610
160.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C.F) (C,F)
0.01 1091.18 87.93 79.67
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(ain):
Chrg ut
(Ib uet):
run
time
(«in)
0
60
120
180
240
300
360
420
480
540
600
660
720
SHEET HOME Units l-metric,
OK- 18 2=English:
ES/CB Y, 06M:
11-18-89 Pitot co:
B-2-4 Gas MH :
Pb (mm, in. Hg):
720.00 Stack area (m2,ft2):
Wood moist (.?. uet):
27. 10 Burn
vel dp
(«,« H20)
(in.H20)
0.051
0.051
0.052
0.050
0.050
0.051
0.053
0.053
0.055
0.055
0.054
0.054
0.053
tunnel
temp
(C,F)
73
85
95
94
94
94
83
81
83
84
83
89
90
DGM
rdg
(m3,ft3)
497.705
528.400
559.200
590.200
621.200
652.400
683.800
714.900
746. 100
777.200
808.400
839.600
871.013
DGM
temp
(C.F)
68
76
82
84
88
89
82
79
77
78
79
81
82
Samp vol
2 (sm3,scf)
1.009 268.980
0.99
28.56 Flou rate
21.82 (dsmSm.dscfm)
0.1963 144.50
18.00
rate (dry kg/hr): 0.84
DGM dH
(nun
(in.
0.
0.
H20)
H20)
670
670
0.670
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
670
670
670
670
670
670
670
670
670
670
vel
(m/nin)
(ft/min)
1060.58
1072.45
1092.81
1070.62
1070.62
Iu81.2?
1091.27
1089.26
11H.67
1112.69
1101.52
1107.59
1098.28
PR
CO
103.3
102.9
100.3
102.0
101.9
99.4
98.4
99.8
98.0
97.9
99.8
99.8
85.49
17.640
460.00
1850.00
dBGM
vol
(.3,
22.
22.
22.
22.
22.
22.
22.
22.
22.
22.
22.
22.
std
ft3)
629
367
263
181
161
263
335
531
543
573
531
601
vs/VfflTs vs ave turnel DGM
ave temp ave temp
(C.F) (C,F)
0.01 1089.28 86.77 80.38
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
03
I
Stv manu: SHEET HOME
Model no: flK-18
Lab name: ES/CB
1st date: 11-19-89
Run no : B-2-5
Tst tine
(min): 720.00
Chrg ut
(Ib uet): 29.30
run
tine
(sin)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
1120)
H20)
050
050
051
051
051
051
052
051
052
053
050
050
051
Units l=metric,
2=Engl ish:
V, D6M:
Pilot co:
Gas MM :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Uood moist <.'/. uet):
Burn
tunnel
temp
(C,F)
73
88
95
98
100
92
86
94
96
95
95
92
92
0611
rdg
(«3,ft3)
873.112
903.500
934.300
965.400
996.400
1027.600
1058.700
1089.700
1120.900
1152.100
1183.300
1214.600
1246. 163
DGH
tenip
(C.F)
69
76
85
90
92
90
88
85
86
88
89
89
89
Samp vol
2 (smS.scf)
1.009 267.627
0.99
28.56 Flou rate
21.94 (dsm3m,dscfin)
0.1963 142.21
14.58
rate (dry kg/hr): 0.95
06(1 dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
670
670
670
670
670
670
670
670
670
670
0.670
0.
0.
670
670
vel
(m/nin)
(ft/«in)
1047.26
1061.89
1079.28
1082.20
1084.14
1076.36
1080.94
1078.31
1090.80
1100.24
1068.65
1065.76
1076.36
PR
(50
102.9
102.8
101.0
99.8
98.5
98.1
99.2
101.0
99.5
98.3
100.8
101.9
dOGH
vol std
(«3,ft3)
22.483
22.490
22.334
22.060
22.122
22.131
22. 140
22.406
22.365
22.283
22.314
22.501
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel 0611
ave temp ave temp
(C,F) (C.F)
0.01 1076.32 92.00 85.85
-------
Method 56 Proportionality Kale, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: SWEET HOME
Model no: RK-18
Lab name: ES/CB
1st date: 11 -20-89
Run no : B-2-6
1st time
(«in): 480.00
Chrg ut
(Ib uet): 21.20
run
time
(inin)
0
60
120
180
240
300
360
420
vel dp
(mm H20)
(in.H20)
0.050
0.050
0.050
0.051
0.051
0.051
0.052
0.051
Units S-metric,
Y. DGM:
Pilot co:
Gas MU :
Pb (mm, in. llg):
Tunnel area (a,2,ft2):
Mood moist Cii uet):
Burn
tunnel
temp
(C,F)
75
91
105
106
101
107
91
87
DGM
rdg
(m3,ft3)
247.222
277.200
307.700
338.600
369.800
401.000
432.300
463.800
DGM
temp
(C.F)
73
79
89
93
94
94
92
88
Sanip vol
2 (smS.scf)
1.009 176.582
0.99
28.56 Flou rate
21.84 (dsmSm.dscfm)
0.1963 141.59
16.62
rate (dry kg/hr): I. 00
DGM dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(m/mi n)
(ft/min)
1051.62
1067.23
1080.
1092.
1087.
1093.
1088.
1073.
70
42
58
38
36
93
PR
101.4
103.
101.
99.
101.
98.
98.
1
5
7
1
0
7
85.49
17.640
460.00
1850.00
dOGM
vol std vs/WTs vs ave tunnel CGM
(m3, f 13) ave temp ave temp
(C,F) (C.F)
21.913 0.01 1080.89 94.22 87.56
22.
21.
21.
21.
22.
22.
046
928
981
941
012
233
480 0.053
85 495.487
86 0.670 1092.78 101.0 22.528
I
to
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED ('- 1 ^ - £ ^
DATE RETRIEVED 11 ""2-0 ~ <$ /
TEST LOCATION Q-"^>
SAMPLER SNff ^ 2 3 '-/
(HG BAROMETER UNCORRECTED)
PRETEST B.P l''£C (IN HG)
TANK "2,1.73 (—IN HG) TEMP
TORR ABSOLUTE -~rr8 ^.~7'/'
POSTTEST B.P. I/. "7 cl (IN HG)
TANK //„ / ^ (—IN HG) TEX
TORR ABSOLUTE 7/7 1 . S
WEIGHT GAINS
PROBE ".7
LINE
CONDENSATE - Z.
- TEST TIME °£> (MHtf)
STOVE ID -1 K\ ~ / 0
WOOD SPECIES Spruce.
WOOD MOISTURE (3 DRY) 17 .'-i^l
WOOD MoiSiURi (% WET)
WOOD CONSUMED (LS) )"7 Cl-l (KG)^fl.
SAMPLE FLOW RATE PRETEST
ROTHXETER IV "(ML MIN) & O
POSTTEST
ROTAMETER 76 ,(>JL MIN)
PRETEST LEAK CHECK
3TART £'.( (IN H30) FINAL 5. £ (IN H20) LEAK RATE 0,
POSTTEST LEAK CHECK
START £.1 (IN H20) FINAL40 (IN H2) LEAK RATE 0 ,
(IN H20 MIS)
(IN H20 MIN)
POSTTEST GAS ANALYSIS
C02U)
RUN COMMENTS:
CO ( 3 )
'?•• C1
GRANS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
MIN. •*•
MIN.
MIN. DELTA
PROBE-f FITTING
SAMPLE LINE
CONNECTOR
I-B-2-7
-------
CLIENT _._£_
ES PROJECT R/}
PARTICULATE WEIGHTS SUMMARY Page of
RUN Ho. OPZ- fi~~*- Placed in Dessicator: Date/Time /A Zo~ &1&
STOVE MODEL No.
POSTEST
'
• WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
Ij-lr &ioit>
(/--£/& /ISS
U-1-*/'-Sd
.11-1%
./£/£/
*^/y
o /Z?L/
— , coo"]
CALIBRATION WT.
WT .AMOUNT -
PRE WT
, X'CJJ
-
-------
I
to
I
NJ
I
VO
CLIENT
PARTICULATE WEIGHTS SUMMARY Page of
RUN No. l/T~ A -"Z. Placed in Dessicator: Date/Time //- Z/-S7
ES PROJECT f\0 If** STOVE MODEL No.
POSTEST
Acetone Lot II
Acetone Sample Voluina 5 ?s
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
/t-*Li&/,*r
ft- -•*-/*£•?*
\W/IZ<>0
HEAKER II
7 /£>
-^Se-
• 053G
CALIURATIOH WT
WT AMOUNT =
PRE WT
WW?
&.<*x*>
fr#0cx>
POST WT
5-0. ^«50
-/7.9VV9
Sb,^«»
ROOM CONDITIONS
RELATIVE
HUMIDITY
/?<%«*.
/ o ^ ^^
•7^5 C2 70
BAROMTRC
PRESSURE
I/- 7
^-7
£/.7
Initials
/*/^
i^i-^k^
LO/f^-
A/ . "-T 1 ''*-<-)
(C)
TOTAL PARTICIPATE CATCH (A-i-IH-C) =.
-------
CLIENT
ES PROJECT
Rf)
PARTICULATE WEIGHTS SUMMARY Pat's. . .of
RUN Ho. p~ Z. Placed in Dessicalor: Date/Time..//- ~U •
STOVE MODEL No. _/) A -
POSTEST
if
Acetone Lot II.
Acetone Sample Volume.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
;/-2/<3v«;
//-Zi/o*-3e
BEAKER II
/) - s^^/
-73, £371
-7^ r637r.
75.^-7^
75*. 5?V z
•6332)
CALIBRATION WT
WT AMOUNT =
PRE WT
*-/7,W?
^..o^-.o
POST WT
^O.OCOt,
vv.'/vvv
ROOM CONDITIONS
RELATIVE
HUMIDITY
K/^?5.
/£<5L£?
BAROMTRC
PRESSURE
7. A *7
Initials
^r^.
^144
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
_ (C)
TOTAL PART1CDLATE CATCH (AiB'C) =.
-------
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page
RUN No. l?>- 2 - / Placed in Dessicalor:
STOVE MODEL No. A k~ I ctf __
POSTEST
_of.
•<-$
\^1 01
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
^\
//-/6-427/V/o
^S)
n~f)0
,S3oZ
.*3oY
• $3o47t7
.67^3
,^3V
CALIBRATION WT.
WT AMOUNT -
PRE WT
. ^Vc'C.
• tj* 1
POST WT
* ^>i-t-1s
.v<*9<9
.y^f T
ROOM CONDITIONS
RELATIVE
HUMIDITY
•2/<%7
/«^7
Vf^ ^
BAROMTRC
PRESSURE
ZA 7
T-S'~>
Initials
i
/JfC'/f
x*icf
/» c/f
I
00
I
(A)
(B)
-------
CLIENT I: PA
ES PROJECT ,RP J23 STOVE MODEL No./#'/<-/
PARTICIPATE WEIGHTS SUMMARY Paye of
RUN Ho. /ff-2-"'^ Placed in DessicaLoi.-: Da Le/Time //-/6
iQi3^)
POSTEST
1 NT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
'/-'•iCV/o 56
I/- iq& IH7.5
If-W*
FRONT
FTf.TKfl 11
/?/T-/25
/. ^^,^3
/•^^^?
r <^S5/
^SIZ.
BACK
FILTER II
A£-/24>
• W)
• W)
*Wl
.6W5
» tti^l.^
CALIBRATION WT.
WT AMOUNT =
PRE WT
v ^crcrt-i
^ ^&Cf
i
POST WT
v ^>&Bt>
• Wil
ROOM CONDITIONS
RELATIVE
HUMIDITY
/ i @>6Y
^Qyo
BAROMTRC
PRESSURE
T-l. *X
1-2,0
Initials
/^<=/e
/*!?/?
(A)
(B)
-------
PARTICIPATE WEIGHTS SUMMARY
P
of.
CLIENT
ES PROJECT
RUN No. $' 2-5 Placed in Dess icaior: Date/Time ll/''7
STOVE HODEL No. A *
POSTEST
'•
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
//-/S(y 11 oS
II- /
-------
CLIENT
ES PROJECT
£PA
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. /3>~ ^ "V Placed in Uess icator: Date/Time,
STOVE MODEL Mo. /$K^ I #
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/-s
ll-ltvmte
I/' Zo&oQ'K
thl-tl
FRONT
n-Tr.TRn n
/^r-/v/
• l^w
^^ 9vi.
.bSbl
'&¥L,-L
t (s l~
CALIBRATION WT.
WT AMOUNT -
PRE WT
v ScrCti
t 5/tvti
i
POST WT
j, c,i
M
1
CO
J
to
(A)
(B)
-------
CLIENT _J
ES PROJECT A 0 '
3
PARTICIPATE WEIGHTS SUMMARY Page of
RUN Ho. /?' *2 " fT Placed in Dessicator: Date/Time //'/^ £*?
STOVE MODEL t\o./)/(-/8'
POSTEST
1
• WT 1
NT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
^"\
il-7.0 (yOCj-yS
It- -zo(3t nyo
\\-1l& OWo
}h 3-^^
FRONT
FTf.TI-.n II
/JF-/*/*)
lt&}t$
/.o/oV
\.OI*L(
1 .o/otf
*&7fi7
*3?/7
BACK
FTl.TKR II
/J^-/^
* 6 S' 7^
«6^7^
J
. 6s-)<;
^-?«^
.
• ^W
•
POST WT
o '^Vrx-'
* ^X/-Zrt>
< 6^* /
ROOM CON HIT IONS
RELATIVE
HUMIDITY
'Z2^7tf
/V^61S
/9^g-
BAROMTRC
PRESSURE
•i/,9
^/. «
Z/-7
Initials
,
/^/^X1
/J,C^
^'^^
I
DO
I
N>
I
l—•
01
(A)
(B)
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Paye _o£
RUN No. n " 2 ' & Placed in Dessicator: Date/Time/'A ^O
STOVE MODEL No. fl l\
POSTEST
1 WT 1
WT 2
HT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/ /-1l &/0^6b
//- ?v(£y/-z3S
Ih t-W
FRONT
PTf.TER II
/?*"-/ 57
*7^3C)
• 7 S 3o
« 7 ^ 33^
• ^^1-7
* 6 ? 3 ~?
*^7«^
,00L/ ^
CALIBRATION WT.
WT AMOUNT -
PRE WT
• ~tc.
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
f\.. . .. . .. —T~> —. /
U Run f JS -7. — f
1
ES Project t
'Wood Heater Model
Operators _
~ I fi
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr) /, C'Z-.") Thermostat Setting_
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
"Z-/>7"7
6/
/o
^>
/''
Fuel H20; Dry f" .u- ~ Wet .
Fuel: Dry Kg Aj. 7-"~
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Ave.
Pitot Leak Check
Static
I-B-2-17
-------
ENGINEERING-SCIENCE, INC.
Client £ /9/) Hun
1
i— •
oo
Time
Sampling/
Clock
// 1f>
/I i^
1
/^#*~
i
i^/^
/C, 1^
l">/^
/3/<
/ff l^
2C'/^
-Z.//S-
2TL/5-
2.3 /CT
Test
:uel
Ht.
(Ibs)
O^
i.O
?•<-
V-¥
7?.?
V, tf
* .V
ff'V
A.s
y-^
?•<•
<,^
3.5
rlue
Draft
(In
n?o)
Oxf'
O,/?
,<>T2
^?1
-oys-
«o?ft
^-•f^
,olc
.OK
• d)"?C'
,f7^?
fOVtf
•"J'R
Af) /2?> Operators /»'^^
3&/JZ Coal
A///
Comments
C<->/d <~^t-f/ <^~^>i/J/r>'
/
P^ /? (>^ <-.«., c/ A » *////./ =• 5?//-^
/7'«-£f /V/'/i A,- 7- JTf. /,£i *
«t?
7«zy Y,y//^,-i-- 5X-^
"t-ln, /f/f, rv /i *.
Ded
Catalyst Temp
Pr<; ntcrnal
27~
I3i
^^
?,^/
7^?.
^2
2_5fi
22{!l
7^/
?^y
^22
Jk?.
Post
-2<-~?
177
-*,-><>
-M>X
•z,V/
'??/
^•4^
* 7 y
-?7Z-
v^y
Right
Left
Stack
Temp .
-i^
^
IX, -j
35T
%sj-
Dil .
Tun.
Temp.
6?
7*r
5{/
9/
s?
5 S
ft -7
5f
^"Z-
5^
9o
9S-
Room.
Temp.
59
t*3
&-*
<^y
-&&
6V
C~L
<^^
{„<,
c\
&K-
?/
<%-?/
-------
ENGINEERING-SCIENCE, INC.
Wood Heater AK'lfj
Date //- /
SAMPLING DATA
Sampling Location r. ,-V<.y>r/ /?<„
Sample Type
Start Time
Stop Time
Hun Numbe r /?- "Z - /
Operator /-»-..-/? o/
0
9 C--
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
time.min Clock)
D /3'f
/^ 3f>
~bj *-/<;
±&. > L/&CJ
(eo ltf;t
75 / -^c>
^O
i2o If/S
l^f) L/q
IGS c'O
/#o id? IS
W") 1t~>
"2./O VTI
?Z^ C'-&
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Z ^"^ -?o
2.7 /*? /^
-^ -^~ -^
"?"?o •V^
-a,V<" ^P
3^/5 /9/-T
Gas Meter
Reading
(vm) ft3
-2 * r>
•37 ^ ^"2-
V ? 6 . 9
y^9 » v
V97* 3
Velocity
Head
( PS). in.
^ e, «3 1/
x o ?y
r«>5S
* f^^>
.Oft' ^
a t1 ?y
« <^^x
Ori fice Pressure
Differential
( H), in
Desi red
H^O
Actual
rf <^'7
-£ 7
-67
r C' 7
.^7
.fcV
,6-7
^< 7
. 67
- ^
Filter
9 V 7
?<^> V S1
7/ V T?
75" ^/
-------
pp™ fp^
hjjaa tlSELTi
L'/^rvi
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (conL.
Hood Healer
Date //-/
Samp liny Location _d
Sample Type <>'G-
Uun Number /I- z -/
Operator
c />
cj //
\. Clock Time
Sampl 1 ng\(24-hr
time, mlnXClock)
T£7> —_ Z2d£
•37
Vto ~2c>/5
V^ -If
-2.2./<>
S^-T -4o
?7r> -VT
<5»S ^c
/;^ z^/^
Gas Mater
Rcadi nq
JVn,) "3
«7 .9
«r^,r, ^~
5g-
*rt^-z.
.o5U
.,0^1.
.6-5-?
. rt
./; -^
, A o
_,LA;2_
--LjL2-
TEMPERATURES
Di lution
Tunnel
Meter
In
W
N)
O
-------
FUEL MEASUREMENTS
Date (\ —\6 ^8°^ Wood Heater Manufacturer
Project No._ Wood" Heater Model
Run No._
Circle One: Pretest Fuel Test Fuel
Fuel Type and Amount 2x4- 4x4 1x4
Ideal Load Weight ; .Actual Load Weight
Fuel Piece Length
Moisture Meter Calibration 12", 22% c?
Moisture Content-(Meter - -Dry Basis)-
Piece No. Readings Average
3 i&j /7o 1^.8
4 c.h*> Ic.e
5
6 < /S.6 /VJr / 1,
7 7.* £^. tr.7.
8 //.I /c.6 //.T-
g &i--e' /f,y IC.L- /#,-?
10 //. L- //,c/ /I.*
11
12 .
13
14
15
16
17
18 -
19
20
Overall .Fuel Moisture Average
I-B-2-21
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client £ PA
Date )l- i k.
Run i l\-7. - Z.
ES Project f \l A
Wood Heater Mode 1.
Operators >-vi e /?
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) , N^ (c Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (8F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Actual Fuel Charge Wt=
Pretest
Z.A7S-
.-v s
c.
,'C-tf // ,r
/
-TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20% Dry | '> / (
Fuel: Dry Kg [
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
Ave. p
Pitot Leak Check
Static
to
I-B-2-22
-------
- z -
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client fcPA- Run I
-> -7
Test Fuel Charge
Page
Date ll~~)(t~&>( Wood Heater Model
ES Projec. I
M
to
I
to
1
to
OJ
Time
Sampling/
Clock
Cd>L/fS
O~f VS
Ogtcje^
O^IG
/O^^
}\ y *••>
/ 2. V *?
/"i_V_5"
H3*Tr-
/5V5"
/rf. V £
/-> v>
/£V_->
i,£> '7f,
(\Df2^ Operators |Ajnrf
^U- /O Coal Oed
Comments
rvp'io - o,r~ cot1 (S HdiV
OBIS (3,1 /-s^i t.t'i.lt*?
/ / y*! 'z>[1///i,'i. - l*> Q
111*1 ri'ifl *jf7 t^l £n2t*
'
/6>eV .<•/ ?, '? •-- Z ,4 * .*?..(?'.lv '
/
-
Catalyst Temp
Pri!
>-t*it-/
/CIS
^'
JlL/
/,tjlj
9^6
7^5"
7S7
^',S^
f^tf/
Surface Temp.
lop
Rear
Do tt oni
'iC-Jf
3T.-7
'T'tJ'j
^/5'/
-------
ENGINEERING-SCIENCE, INC.
SAMPLING OATA
Wood Heater
Date II-IL-
Sampling Location
Sample Type
Run Number_
Operator
C.ft
-2.-
Amblent Temperature
Barometric Pressure
Static Pressure, (P^T
Filter Number(s)
Meter
Start Time
Stop Time ____T__^__
Probe Length and Fype
Pi tot Tube Coeff1c1ent_
Assumed Moisture
Sample Box Numbe?" /
Meter Box
Meter
•>
/•-*
H
(,COL1
Pretest Leak Rate . QQ z. CE? /o '•
Post Test Leak Rate ... <-r, 5^-0, fo ''-
Read and Record All Data Every h-(\ Minutes
1 Clock Time
Sampling (24-hr
t1me,m1n Clock)
£} &{£* ^^
1*
'i"^
C,o o7(^>
(ef\ ? ^
-)/}, $
7VV .7
"7 "7/^ • *V
-^7 — ~
Vel oci ty
Head
( Ps). In.
H?0
D.O'i'V
, O5
. t\5'v
. o£^
. O"5Cj
,. o ti 5
., o 5' <:•
. <~> "?-/
f o*y^
., 0 c/^
0 * /
. r, 57
0 C7 5" 7
.or, -7
c>5> ^'
, 0 ^
Ori fice Pressure
Differential
( H), 1n. HzO
Desi red
• C-7
Actual
• <~p~7
<-> 7
.<<,-,
.£.*") •
<• "7
,Q»— >
• C. ~j'
. Co-7
.
« /. -9
t_^*7
» "7
. /,-•»
.6 Y
, /,•> 7
, A 7
«.'• "7
~' ")
Dilution
Tunnel
TEMPERATURES
Meter
In
~T~\
£*3
^i"
<3 7
. -a"/
9,'V
Meter
Out
7 TS
So
5 S
^s
•ay
•s ?
Filter
Implnger
67 6' 'S'S
7<^ • ^T?
76 <>" <7
S_iL 1
Pump
Vacuum
1n. Hg
?__
>
>_
2.
2_
•7
Flue Draft
1n. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
/I K
Vlood Heater
Date //- /
__ _ s
Samp Ting Location ~7G • co
^>c;o i <
Vof 3o
V2tf y2,VVO
^S
5V o 1 5 V 5
55S
570
^as
^oO (6^ ^
4.5
61/0
6V5
66.0 IT-tS
67S
/*9«o
-?^c;
Gas Mater
leadi ng
S39-^
P-,7o.-j-
. ^ -5"^
.05^
;05O?
. 0 5c,,
*o5^
c o 5 £
.0^5-
.c^<-
, « 5 ^ <:^
Ori f ice Pressure
Di f ferential
(All), -in. ll?0
Uesired
Actual
,6^
-C--7
.^7
.. ^ 7
.(* -7
•6-7,
-c.-.
-^ I
i~7
.Co -/
• C--7
.A 7
• &>-)
-67
• 6~?
.t-*-)
. & 7
« <:»?
.67
.6 7
. 60
V (f~1
• I- 7
TEMPERATURES
Di lution
Tunnel
Meter
In
Stf
clf
S9
^^
tf*
Muter
Out
3 ^"
ay
8 S'
^^«
T?<^
Filter
« X
B-l
^<^
7tf
7^
Impinger
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (conL.;
Hood lleater_
Date //- It
Samplimj Location_
Sample Type_
Run Number^
Operator /-t-;
//
\. Clock Time
Sampl1ng\(24-hr
time, min\Clock)
^^" — — /-i_io__
?Zo /-SV5
93^ w
-7^o /^7
76^" 3o
7?c? /-5V5"
7^-f .c^
^ it
«?
Wo Z^ V5"
Gas Hater
(eadi nq
(v,,,) ft3
q 9 6- » 7
/o 2. 7 . l/
, --. Tt-J t~t
/Tl i VV /
ios<).ns
Velocl ly
Head
(al's) in.
ll?0
,. o ^ (,>
., /> <~> C
* o <\ <-
e ^^6
,. ,. iy
)ri f ice Pressure
Di f ferential
(All), -in. ll?0
Jesi red
Actual
. 6 1
• (• 7
, C- 7
, /:. -7
, /;. •;
^; 7
*i-7
,/-T
,<:. 7
TEMPERATURES
Ji lut ion
Tunnel
luter
In
%<; •
^ '/
S^
-
Meter
Out
_Ji£_
fj 3
5^
Miter
7f,-
7',~
7<.
Impincjer
^"7-
Tv .
S?
-
'ump
Vacuum
in. Hg
?
->
?.
Flue Draft
1n. H20
I
w
I
fsj
I
10
-------
FUEL MEASUREMENTS
Date //-/£-3 ? Wood Heater Manufacturer
Project No. £^/Z.^ Wood* Heater Model ATZ^•'
Run No. -fc-? - 2-
Circle One: . Pretest Fuel • x
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run t
ES Project f
'Wood Heater Model
Operators I u H
Alt-/
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr}
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audi t
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
Z./.5"?
/<-/
o
ft. G /'?<'•!
f\jA
Post Test
I/, 7V-
£7
/ ^
<7
/c.p //o.n
' .
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H201 Dry
Fuel: Dry Kg
to
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
p Temp
A 1 B 1
2 2
3 3
4 4
Ave.
Pitot Leak Check
Static
I-B-2-28
-------
ENGINEERING-SCIENCE, INC.
Client b \^A
Date
((~l~f- &CY
WOOD IIEATEH CEIITIFICAT10N TIIST
TEMPEKATUUE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal lied
ES Projec. I
Wood Heater Model
Operators
.
Page
_L»r_
I
en
I
N)
I
N)
Time
Sampling/
Clock
#•30
(>*> 30
// 7*0
TV
1 (<>-*, o
•Zo
Test
Fuel
Wt.
(Ibs)
(2. <-l
"7-7
/ K.
Flue
Draft
(in
Comments
H.l/z.t-
- ;;
/)//< /
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date l
SAMPLING DATA
o
Sampling Location GTS
Sample Type <,'<=j
Run Number ~p> - 2- - 3
Operator
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter Y
/.ck.-L/
Read and Record All Data Every
Start Time
Stop Time
Probe Length and~Type
Pi tot Tube Coef fident_
Assumed Moisture ;
Sample Box Number_
Meter Box
Meter
/2,
H
Pretest Leak Rate 6.06'
Post Test Leak Rate , ^2.
Minutes
13-
(ftf
Clock Time
Sampling (21-hr
tlme.min Clock)
O 6 Q> "S rj>
15
r?o
^"7
^e> 07 3 o
71
ro^
/?o (o'-V^o
(.is
/!?CJ
/^s
/So ^°f 3o
/ "7 ^
1/0
"}~"S
•) £fO ('O-'-icj
'2-SS~
77^
i-66
T-io 1 / 3O
"sis
-)^0
\^2^ T^r^T^
Gas Meter
Readl ng
(vj ft3
flt o.So 7
CftO: <-/
/ Z./. -i
/fZ. 7
t &*-/ 7
~> / •*;> *"}
^vTST^T
Vel oc1 ty
Head
( Ps). in-
II20
c.oS.5
^ —
c' » O "5^5
fi . O 4> S
(X^'S's
6 . 0*7 -/
0,os3
^ O 6 ^
(% <55 2_
. ,O'? ."i
. o 5 '?>
. o'y'i
,o 5V
t 0 ^^
„ (7 ^^
Cx £5 C("
, O x>'V
e> 5 V
. C 'J *>
. 0 S V
v C>"r,'~/
J? c(, <^/
Ori f ice Pressure
Di fferentlal
( II), In. H?0
Desired
. .-. 7
Actual
'• 1
.(A
.f, -7
. 6 7
• £• i
6-7
•(••* ~?
k —-,
I C'~?
(i>~f
I (.'• 1
. £, T
°& 3
• & 7
.(--)
-•7
67
G ~7
/•„ -7
^ t~ 1
. <', 7
- t-V
TEMPERATURES
Di lution
Tunnel
Meter
In
^^
c; ->
9/
92
'Vc'
7B
- <& ^
Me t e r
Out
-j &
-~) —f
'C> ~7
9 2-
*ifi
"77
^^
Filter
Implnger
— ^
Flue Draft
1n. H20
DO
I
NJ
I
CO
O
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (corit.)
Wood Heater
Date //-
Sampling Local ion
Sample Type
/&.
Run Number /? -Z
Operator j>lj c. ft
\. Clock Time
Samp11ng\(24-hr
time, mln^vClock)
-2,67; — ~n^
V> <*o
tot JC
vto /-vte
v^ ^
Y.5H of
IbS IS
vtr
$56 V^
<;7 <^'
S^ /^
J^-e> ti.^0
6>t^ V^
^.?0 tf<3
/730
^76- V^
^ 92 .. 3
Veloct ty
Head
UPS) in.
HpO
O.o5 I
- 5-Z-
^ o 5 -L-
.^5Z
^f'^3
f o<7l.
. 0^0
< 0 ^i
. C! 5-Z,
- r, S -i.
ttiS)
t()C,\
,o$2-
4 0 ^i-
of> 5/
• o 5 o
Ori f ice Pressure
)i f ferential
(ill), -in. II20
Desired
Actual
.6,7
.6 7
,6-?
>67
»&-7
;&-)
.67
a&-l
c &> 7
.t>-y
v 67
.(.-7
* £--?
^ 6 •)'
^ 6 7
- £:> 7
, C^-7
• 67
/ 6"7
- 67
, 67
^67
.f.-7
, TEMPERATURES
Di lution
Tunnel
Meter
In
•77
9;^
S/
55/
^V
Muter
Out
->-*
B o
7
I
OJ
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
6-2-3
Hood Heater
Uate ;/
}< - /
'>
Sampling Location C1 /f. ^ /
Sample Type f>&—
Run Number /%*- Z - "*>
Operator/i^ <- /' /L; /?
'X. Clock Time
Sampl 1 ng\( 24-hr
time, m1n\Clock)
'7?K ~~~^^
72& -/31o
735" V5
•7C
1^ I *
-7^ <•>
' 4 ClS'f)
J f $<>
„ O$\J
t 0
,^7
,6-7
* 7
< f0")
,(«7
• (*'•!
TEMPERATURES
Ji lut ion
Tunnel
i
Icter
In
•5S
32
c? .
<£n
-
'ump
Vacuum
in. Hg
-7_
-?
?_
Flue Draft
in. H20
-------
- Z-
FUEL MEASUREMENTS
Date _ \\-\7' g i Wood Heater Manufacturer ^-^zz^
Project No. £.\>i"L"S Hood" Heater Model _ A- i/ - /'
Run No. TV -"•> -"~^,
Circle One: Pretest Fuel • XTest F_ue
Fuel Type and Amount 2x4 _ 4x4 ----- """1x4
Ideal Load Weight _ ; _ .Actual Load Weight _ "
Fuel Piece Length _ _
Moisture Meter Calibration 121 _ 221 _
vJ0* d T< ~, a. °F _ • :
Moisture Content-(Meter - Dry Basis)—'
Piece No. Readings Average
3 CiZ M^ J±'f
5 f(-_B_ lii>_ FI.&
7 ^^- 27^I_315_ 3Z.f
8 /7o H,\ J7?
9 tSl_ ffS_ /££
10 ^-^^J_321 17^
11 iv>y y/.?' 3y.^
12 "zL'tC '$i-,0 1^t
13 /|.2 I2SJ rtSi
14
15
16
17
18 _^_
19
20
Overall .Fuel Moisture Average ~LC, "7.1
I-B-2-33
-------
Client
Date
HOOD HEATER CERTIFICATION TEST INFORMATION
Run t
Wood Heater Model
£5 Project f
Operators C-'-i MrK- . — iVv f\
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
~?(.~f-7
7t-
/5
O
/C.C/:'L\G
MA-
Post Test
T-/.<<'£
6
-------
ENGINEERING-SCIENCE, INC.
ClU'nt r^V^A Hun I
WOOD IIEATEH CEUTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page / of /
Date U-lP-^l Hood Heater Model /}\<-l'?> Coal lied
ES Projec. I
M
1
to
1
NJ
U)
Time
Sampling/
Clock
68<~vf>
fFf£>c?
/OS10
//OO
/"Z ^
y 'i)^rr:>
1
/fj fi*.
/7<7n
/f &(,
Z-C^O
Test
ruel
Ht.
3. ft
'^•7
/A2-
-7.2
•^ 2-
^/•ei'
/2 .1
9,9
»9
^' -cf
V. 7
Flue
Draft
(In
H?0)
().(tJ 7
ttC^^t^
.oW
^-, ty^y
tffrt-
«(>~i>~}
t-c>3c.
,tf>'Z",
, f,?Cj
• L>2.")
,.<-'l~i>e>
•C'~lif..
ix^tUTS Operators /l4f/{ £-L> /•/
Comments
7.' /1ft "I.-** «•,-,,. M-,^ ,',^.^
f> n'f.f' v -'M> ^Jb./\t»x
ip.^i/y. 2- / (. 7 /*• c,tt c*. i ( j rt . x>
/ t(*<> 1J7 /!*>*& "//.'?*'
/ 3^9 ScT/n-' ^ /"
/ % /I yj l >1 Tr. fH /> >
Catal.yst Tenp
Prc
••/?/
r-ov
^i^
ffi
&LC'
6?fv
*i )/'
C,£,&>
nte'rnal
Post
->v(>
77'
?*//
7/9
/j'9S'
^/<:
6>flY
Surface Temp.
Top
Rear
Uottom
? 2 ~7
'•'V>"~7
^O "7
v.'Tv
V //
"?/ 5"
'?
-${/*,
ZZ7
J ? S"
"Z^S
Oil.
Tun .
Temp .
~7 "^
ft'S
9^"
V V
c^y
W
S 3
S1>
5f
S "~?
55 9
fo
Room.
Temp.
7?
<•>*/
(s 3
6
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
Sampling Location C."/\
Sample Type j~> (-]
Run Number_
Operator
-o ( X
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter ,
SAMPLING OAFA
—>
Start Time C \s,
Stop Time ^___^
Probe LemjtTTandlype_J
Pi tot Tube Coefficient
Assumed Moisture
Sample llox NumbeF~ fc
Meter Box Number/jj,?,.,/ jj
Meter II
Pretest Leak Rate
Post Test Leak Rate
<£
Read and Record All Data Every (,-U Minutes
1C,
/o
Z
1
NJ
I
Clock Time
Sampling (24-hr
t1me,m1n Clock)
O (~> P^° *•'
15
3o
4<<5
6O G-JOL>
75
1O
I&5
\lo |ooo
/°>S
ISO
1'S'i
I9O [(oo
/"H
7?6>
2 1 -.3
2YO ( 2oc>
"''i'S
'70
2^^
,7 ,^ . '>. ^
"\l*>
~v;o
'i'/*)
',^c-f* '2^
'>"?o, "Z.
6 2 /„ 2.
^,^2,f^
&f<3.<2
Velocity
Head
( PS). In.
H20
d 05 /
O,f \S ?_
,OS 2_
. 09 ^
/(7 ^^
« ^- ^
» 0<^ I
• . 5 V
.Os /
,050
,<^.'.SO
.. t>c,c>
* o 5 /
c3 t' •? / '
t o 6' /
-oSI
, 0*7 ~}
*, 0*3 ~s
0 r, r -3
Ori ficc 'ressure
Di f ferential
( H), in. H?0
Desi red
- f ;- 7
Actual
•(-7
.6-?
(j-'~7
, & '7
,6-7
,^,-7
t & /
,(,, -?
• 61
. ^ 7
• 6 7
. 6 -7
.6-7
, 7
^
^>
ij_
C
2
1,
-z.
Flue Draft
in. H20
-------
SAMPLING DATA (cont.)
Wood Heater /) /<
I
N>
I
ENGINEERING-SCIENCE, INC.
*
Date
//-/?- 5*7
Sampling Location C f r^Yf d &.VY ?
Sample Type 5" <
f~
Run Number /?- Z V (7 <~i ^- -?
• \^ Clock Time
Sampl1ng\(24-hr
time, min^vplock)
TT?>"cr — -i£go
**>T? • )*~?
"?9o 1e>
tJ sy ^ ^/^*
'y?^* \^tst/
tl"}^ , f~
IS&' *?£>
L/b'C, L/<$
4"3 O Jd, Of,-
£yQ £} i c
6/0 3c-
SZS ^
^o n#v
£%T') rf
S?o 3&
*?SC ^
£,(> t&
<£S/
. o 5V
> o 5"3
« o s y
„ 03-5-
- o ">T>
* o5~y
• o$y
a Ci^1^
a O £V
» c) 9 '3
o r> d
^5y
.. <^5^
«• (9 5^3
. o'jJ
Operator
Ori f ice Pressure
Differential
(all).-in. ll?0
Jesi red
Actual
» (f 7
, ^ "7
,0 -7
-£ 7
-/^i "7
, & -j
> C ')
«<£>"}
• 7
*67
.<£7
•
-------
FUEL MEASUREMENTS i_> c_ /
"5-Z-^
Date _ ( • "• (c " 8 'T _ Wood Heater Manufacturer .oaL. ~UJ^Q
Project No . A lx / 7 "•% Wood" Heater Model _ A-UC- t fc^
Run No. _ ~T> --> -i-i _
Circle One: Pretest Fuel
Fuel Type and Amount 2x.$
_
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length _ . _
Moisture Meter Calibration 12% _ 22? _ "Z-"^ . f
U/c-c-c/ TV T S. °F _
9
10
11
12
13
14
15
IS
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Piece No. Readings Average
i ^" za/ ->n zo.y
2
3
4
5 2$^ -QSJIJ.
6 lc-, /o,$ IL~L
7
Overall Fuel Moisture Average
I-B-2-38
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run I
ES Project t f\
Wood Heater Model
Operators i/
Akl-V
, ,l/M<-R
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) _ Secondary Air Setting
Achieved Burn Rate (Kg/hr) 0,
Primary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
£ /, c' (r
~7T_
~ £
o
iC.O /lC O
/\|A-
Post Test
2 y,9/-
-7V
/•?
O
/<:- ,i< //c,o
'
TEST FUEL DATA
to
Actual Fuel Charge Wt.
C\ -">
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20i Dry H.i'
Fuel : Dry Kg I
LOADIN6/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
to
Met
L-
I-B-2-39
-------
ENGINEERING-SCIENCE, INC.
Client p pA-Hun »
WOOD IIEATEU CEKT1RCAT ION TEST
TEMPEIIATUIIE AND FUEL CONSUHI'TIOH DATA SHEET
Test Fuel Charyc
Page
of
Date IKI*7-£»cf Hood Heater Model I\K_-I B Coal l)ed
ES Projec. 1
M
1
00
1
1
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Time
Sampl i ng/
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Test
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Ht.
(Ibs)
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6 .9
v * V*
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Flue
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(in
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Coininents
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Surface Temp.
Top
Hear
Uottoui
III
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T./,^
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277
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Kight
Left
*
Stack
Temp .
l( ~>
'"b>T
Cjiy
9<1
O ^
7/
1C-
7V
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
(L.
- s
Sampling Location
Sample Type
Run Number
Operator
Ambient Temperature
Barometric Pressure
Static Pressure, (Pj
Filter Number(s)
Meter )(~- T
Start Time >~>O
Stop Time
Probe Length and Type . /<-/. '
Pi tot Tube Coefficient .;/-?
Assumed Moisture ^/
Sample Box Number
(-liter Box Number _/<,
Meter II
Pretest Leak Rate 0.t\O ( <
Post Test Leak Rate^,^c> /
— „ /o
&? //
If
Read and Record All Data Every C o Minutes
Clock Time
Sampling (24-hr
time.mln Clock)
O O&fjC^
i<5
-^«r>
V5"
h-O ftc/'
-7^
CW
/cC)
/•>fj [OV*-^
l~\^
lLJd
Xr^
/po i^v
AH
i-IO
lls^
Z^l) (Itf
~i£>ct
•71O
•^O ( -*)rLj
!bir'
•\^tj
rj^'
^1,0 IHW;
Gas Meter
Reading
(\) ft3
96 ?> 5
c/ 1 c/ '"S
9^v
cj 2-7. 6
t'L>tt. ~1
Vel oci ty
Head
{ PS). ^.
H?0
C.OS'O
O.r.S /
.•^•5t:>
. oc, o
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. £'£> Ci
, O ViO
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» f'5"/
• t 0 S )
'* 0 ^ /
•0-3?.
, OS Z.
.«&/
, o S /
. 050
. 65 /
,&~? /
O cj /
<;•,«•;/
, f.-> /
i < ] ;') ?
Orifice 'ressure
Di fferential
( H), in. ll?0
Desired Actual
, 6-7
• C'i7
, Co '7
. (.-. —7
,c-7
. 6 7
.<:• 7
,67
-IT 7
/ O7
• (f '1
c S, 7
.d- 7
, ^ -^
. /* -7
. (* 7
• 6 7
, (* 7
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To
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Filter
b{-
Impinger
G <^^ .'^
-7 1:> <> 7
sy 5V
%'$ • 5"P
j-i1 d- >V'
7'.; T7
Pump
Vacuum
in. Hg
•-7
t _
73
^
'2,
7_
-------
SAMPLING DATA (cont.)
~E>-z-5T
I
CO
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I
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tinea ^XZLSH)
ENGINEERING-SCIENCE, INC.
Hood Heater AK" I O
Date
Sampl i
Sample
II - \c\- r-,'n
ng Location c _K
Type
^> (~i
Kun Number 7^ - 7 ~ ^
Operator (_^>u*( . _\ b\ K.
\. Clock Time
time, min^Xf-lock)
~ ' — — —
t~>,~}^
3'?<3
-Yo5
t/l-O (<^£><^>
43^ ISL_
tfjo 30
JsL^S_ '-/^
t-/$o J6, v-v
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c,iyo fl *"°
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5~~)a ~$&
56? W
6 ^^ / f> 01?
b/^ " ) '-t
6>~lo ~>,tJ
6,yf /yf
fnh£> /*! f?
le'7£j l*>
fcclo
^v? y^
Gas Mater
Readi ng
/ ^ i5 f * /
i / 7 £j ^T
t/S2. I
1 /ft ~llj
12. 11-/ Cy
Velocity
Head
(Al's) In.
H?0
£>, c 55
• Cj^-) C^
.^S O
c O $ /
, 0 S' /
, O'D /
i oSi
f e>'6 ~~L
, t35~il
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.oS/
« So
c t *? /
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„ r> TO
j ^5^
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. c'J/
Ori f ice Pressure
Di f ferential
(All), -in. ll?0
Desi red
• 4- '7
Actual
• if"7
•& 7
.6.7
-07
(* 7
• ^~?
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,
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. ~7
* ^> 7
" KJ X
-<^ "9
, ^ "7
,<£ 7
' (/^ /
• (.-' "1
, £, -/
f t? 7
TEMPERATURES
Dilution
Tunnel
Meter
In
^7
15 S'
•^o
9 2.
9;
-
Meter
Out
9 6"
S<^
S' S'
^•*?
% 9
Filter
8 ^
Q /
O ^/
3 *5"
3 "c.
Implnger
^ 0
So /
<£~^
^ <£
-
67
'ump
Vacuum
in. Hg
"2,
'Z
7,
2,
Z
Flue Draft
1n. H20
2-
-------
TVz-s
FUEL MEASUREMENTS
Date H-)^- '22>'7 Wood Heater Manufacturer --
Project No £ N I "2. ">s Wood" Heater Model A-] - ^ ^=
Circle One: Pretest Fuel • Cjgst Fu&>
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; Actual Load Weight
Fuel Piece Length
Moisture Meter Calibration 12i 225 "2-3
Moisture Content-(Meter - Dry Basis)- CorvecTcd.
Piece No. Readings Average
2 /C.5 iS-l JO-S
3 i'±_ l±2 <-'c'
4 /;.j_ ZM 2LQ-
^-
5 -ju.^ 25'Z- '6.S 2.C. (
6 6^.2. 3/,S 37,6
8 / -5 ^
10 /£/2 2iF
11
12 .
13
14
15
16
17
18 .
19
20
Overall Fuel Moisture Average
I-B-2-43
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run I
ES Project f
I?
'Wood Heater Model
Operators
A!/-/
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr) f, Q {.
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings _____
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (eF)
Cold Draft
Firebox Volume (ff?)
Fuel Charge Range Wt.
Pretest
•2.1. •?•-•
/o
o
/<><£>//£>. 0
AJA
Post
Test
T-A7V •
9
fv,e> //r, . a
/
-I
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
to
Actual Fuel Charge Wt.
Fuel H20% Dry l''/iV Wet
Fuel: Dry Kg j*, i /1
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
I-B-2-44
-------
ENGINEERING-SCIENCE, INC.
Client fr 'p/^| Run
WOOD IIEATEH CEUT1KICAT10N TEST
TEMPERATURE AND I:UEL CONSUMPTION DATA SHEET
Test l:ucl Charyc
Paye
of
Date U-?6-P/7 Wood Heater Model /\)(-/ 8 Coal Ued
ES Projec. f
M
1
w
1
NJ
1
Ol
Time
Sampling/
Clock
01VS
O3cz *7
rt^^/S"
/ o V <^
// -/ S
/3V5"
_/.*/*/ *?
/ ^V *5
Test
Fuel
Wt.
T-7
•y.ff
/c^ , ^
^ c/
'T C*
7,4
5". (f
Lf 1 *?
y •(•
Flue
Draft
(In
b,02O
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6.052.
>c<-/cf
« <•.• L/ s
C3£/
-»£> ^£1
tO~£c*
id 1 7
f^J/i^'S Operators ), ^('/-l , Jinc^s
• (
Comments
"7. "//.S. V £/^'"' ^'iiM-'-, '••<-!;*•>•('
(b; d B/1 1._ /\T ."' • ^^X
VV.y / 3 ^ tO-(rfla-'f
/'•>!
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^V'^l
/(,/
Surface Tenp.
lop
Rear
Dot tow
'2-~i-c^
'*>'?<»>
V/O
*y^ ^
'/ ^
1/^3
"*2 J Cf
£,- £f Cf*
2~i~t-
Right
Left
Stack
Temp .
V.OZ.
T"6y
^1 T> (_/
— •£ ^T */
'?<-//
"^ 7
22 /
/ 7"?
/V S"
Oil.
Tun .
Temp .
Y(•/
/&~)
9y
,? 7
S
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date i~i
SAMPLING DATA
z
O
Sampling Ldcafion
Sample Type J5 c?
Run Number /? - 2-
Ope r ato r MH/-I
Start Time
Stop Time
o
-s
Ambient Temperature'
Barometric.Pressure
Static Pressure, (PTy
Filter Number(s) "
Meter /'- ,
Probe Length and Type
Pi tot Tube Coefficient
Assumed Moisture *-
Sample Box Number
Meter Box Number
Meter II
, V V
Pretest Leak Rate
Post Test Leak Rate 6 ,
c!>.o<-o
7/
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
& & 7
<-/^
/\c> O *P>
/£*->
l~2C^> (X/V'-"'
/3S
/5"O
/6?
A^O /£-V '"'•>'
/VS
Z/o
225
2VS
^-7O
2.&i;
•^,00 / .•> <:/ ^
•^(5
1 •>-^->
Gas Meter
Readi ng
(v,n) ft3
IV 7. 11-L
Z-7 7. 2_
A? 7. -7
1 3 3 / /^
3 <£ 9, ^
1o/.f)
Vel oci ty
Mead
( PS). I"-
H?0
(3,OSt^>
o.oSV'
c-. , of>i.. .
, <^^ i->
, O^O
. <-^ScJ
tj. 5o
. (j^5o
U S H,'
O c~i e i
0 S'C,
, ci'So
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(. <^ ^><1
c (t *~~) O
a n <~} }
o C< f> 1
* o $"&
e O *} O
a o ^r /
f c) ^~~£
* ~~?
.6-7
. ( , 7
.67
•C.7
, ^, 7
_ < i- ->
.C 7
. £• ^>
- /• 7
-57
S1'/ .^'/
S^ -T7
•x^ 5"^
S S"
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
/I /< -
Wood Healer
Date ;/~ ~Z o -
Sampling Location
Sample Typo 5'Cr'
Run Number /%- Z -
Operator
Wo IH VS
VK- /S"9
Vel oci ty
Head
UPs) i"-
ll?0
„ o5"-l
- n^i.
..05--L
. o 5/
» fS'1-
j o <^i "v
,041
t-*$5
Ori f ice Pressure
Di f ferential
(All), -in. ll?0
Jo si red
Actual
. ^7
.<5,~?
^*?
*^i ~?
• <^T
.^."7
, f,~~)
,(*7
)i lut ion
Tunnel
TEMPERATURES
later
In
X?
XX
-
Muter
Out
X ?T
?f
Filter
79
7^
Impinge'r
SV
^^
•
'ump
Vacuum
in. Hg
7_
7L-
Flue Draft
in. H?0
I
ro
I
-------
. "B-z-c,
FUEL MEASUREMENTS
Date ''~ "2-*—' ~~^ ' Wood Heater Manufacturer SiOee~r
Project No. rx S 12- "^ \ Wood- Heater Model &U ->
Run No. ~~2.--> —<^a
Circle One: Pretest Fuel • Tgst FueJ
Fuel Type and Amount 2i\ ^x.^ lx*>_
Ideal Load Weight ; .Actual Load Weight ~
Fuel Piece Length .
Moisture Meter Calibration 125 225
vJoed T< "i O. °F
3
4
5
6
1
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Piece No. Readings Average
1 65" /'* ^f
Overall Fuel Moisture Average
I-B-2-48
-------
TEST SERIES
B-3
-------
TEST
B-3-1
-------
Method 56 Proportionality RatQ, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
OJ
I
Stv manu: SHEET HOME
Model no: RK-18
Lab name: ES/CB
1st date: 11-30-89
Run no : B-3-1
Tst tine
(min): 572.00
Chrq ut
(Ib uet): 16.60
run
time
(min)
0
SO
120
180
240
300
360
420
480
540
572
vel dp
(mm H20)
(in.H20)
0.048
0.050
0.045
0.046
0.046
0.046
0.04?
0.048
0.047
0.046
0.046
Units l=n«tric,
2=Engl ish:
Y. OGM:
Pilot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Hood moist (.7. uet):
Burn
tunnel
temp
(C,F)
87
86
83
90
91
94
89
90
83
84
82
DGM
rdg
(m3,ft3)
551.611
581.800
612.600
643.400
674.000
704.800
735.900
766.600
797.500
828.800
845.811
DGM
temp
(C,F)
79
83
73
81
86
88
85
85
81
81
81
:====^=======__===
Samp vol
2 (sir,3,scf)
1.009 210.597
0.99
28.56 Flou rate
21.78 (dsmSm.dscfm)
0.1963 136.34
16.89
rate (dry kg/hr): 0.66
DGM dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(m/ftin)
(ft/nin)
1043.30
1063.84
1006.47
1024.13
1025.06
1027.84
103-1.26
1046.15
1028.59
1018.53
1016.65
PR
C/.)
97.
95.
103.
100.
101.
100.
99.
97.
101.
103.
1
9
6
8
0
4
2
5
3
9
85.49
17.640
460.00
1850.00
dOGM
vol
(m3,
21.
22.
22.
21.
21.
22.
21.
22.
22.
12.
std
Ft3)
761
038
243
976
917
050
886
029
479
217
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1030.44 87.18 82.55
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED //-?.? - ?'1
DATE RETRIEVED
WEIGHT GAINS
PROBE '
LINE
CONDENSATE
— TEST TIME_
TEST LOCATION C*(*,7*9 "(ML MIN) ^ /
POSTTEST
ROTAMETER
/^ C, S" TORR ABSOLUTE "Z, 7^ 5, "2—
PRETEST LEAK CHECK ~
START7.. / (IN H20) FINAL^^ (IN H20) LEAK RATE Pel— (IN H20 MIN)
POSTTEST LEAK CHECK
START
-------
CLIENT
EPfl
ES PROJECT /{[) /"23
PARTICIPATE WEIGHTS SUMMARY Pace of
RUN Ho. I//J-' P~3' /Placed in Dessicator: Date/Time //- 3o - %{
STOVE MODEL No. /? K '
POSTEST
•2330
;
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
12- 1 & lo^/c-
IT--, eJ/SoS
H-l-fl
PROMT
5^-^-7
-/Z?o
*/2.X/
.1*1.1
,/Z^3>
-0^o^
BACK
FILTER II
« i1'6
*/t/Y
i i ^~ * f
.n,-,
' A &&£" ~5
CALIBRATION WT.
V|T AMOUNT -
PRE WT
. $<*«
41 J OO&
POST WT
, $*<-o
»' fic/t-C
ROOM CON D IT IONS
RELATIVE
HUMIDITY
rt&t,-)
/
/*K/^
w
I
LJ
(A)
-------
ft
PARTICULATE WEIGHTS SUMMARY
Page.
.. CLIENT
ES PROJECT 9\0 /13 STOVE MODEL No. /)/<•
POSTEST
RUN Ho./y/y-^- >-/ Placed in Dessicator: Date/Time./?-/-?'-'?
Acetone Lot ll
Acetone Sample Volume
' -7S
•
WT 1
HT 2 .
WT 3
HT 4 •
WT 5
FINAL WT
I
TARE WT
NET
DATE /TIME
/2- / 6^ '2fS
/2V G> /tf Z ^
//-V~^^
BEAKER II
X)^^
77-7^^
77, •? 36^
77.7 l^R
•^7.73eo
0 00 , OW f
^>0 , c'C'O "Z-
POST WT
fotewt-
*>OsfOC> /
ROOM CONDITIONS
RELATIVE
HUMIDITY
/#<^7.
/?%$
BAROMTRC
PRESSURE
Z A-ST
^/'^
Initials
/^'^
/M
-------
CLIENT
ES PROJECT
/?
PARTICULATE WEIGHTS SUMMARY Pays of
RUN Ho. o~ S-/ Placed in Dessicator: Date/Time I1~-f- ^ *f.fe
STOVE MODEL Ho./3/< ~ /5T
Acetone Lot II 9//S
POSTEST Acetone Sample Volume.
70"
WT 1
WT 2 .
WT 3
HT 4 .
WT 5
FINAL WT
i
TARE WT
NET '
DATE /TIME
li-'(& I2.4S
JI-/&/120
//-V^SI
BEAKER II
^-9^
"7C-.9^/C
76,?Sr/7
7 £ , 9 * / -)
l&^l&l
f 0# $"£
CALIBRATION WT
WT AMOUNT =
PRE WT
£0 1 •fi-vz, /
So, ft-C (L
POST WT
ft> .
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT .
ES PROJECT
O
HUN No. C<£-fi-3-/ Placed in Dessicator: Date/Time /?-5o S9
STOVE MODEL No. /P k *- / ^
POSTEST
23
1
• WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/2-/^/2#S
/2-/fe?/g/e>
//- y s °\
FRONT
FILTER II
/U~-/?i9
»6"?V?
,^7V£
*67V7? OOO ^
CALIBRATION WT.
WT AMOUNT =
PRE WT
* 5*x<*
«1 JOC-C/
POST WT
e ^C'r-O
. '/<7<77
ROOM CONDITIONS
RELATIVE
HUMIDITY
/S^7
f^^
BAROMTRC
PRESSURE
^/.*t
ZAS
Initials
,
x?/cx?
s*
(A)
(B)
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client /
Date //-
£S Project } A Q /"Z "3
TEST RUN INFORMATION
Wood Heater Model // /< -
Operators /MC- /^ £(_)
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr) C ,6r?O Thermostat Setting ,\jA
Primary Air Setting /
Other Settings
£-
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (i)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
"2. /, «r 0
^ ?r
n^
a
1C Q//I; 0
0^/L
o, oca
Post Test
7. /, 7 >!fy ,* //«/Xj Air Settings
Door 6^ y2f / ^ / /4< / /f<- Comments
Veloci ty Traverse
Ave.
Pitot Leak Check
I-B-3-1-7
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client /r~ />/) Run I ft- ^ - /
Test Fuel Charge 11, fr"*-
Page
of
Date I/- ^-89 Wood Heater Model /)/<-/<& Coal (led '2,7?
ES Projec. f
M
w
1
1
1 — •
1
Oo
Time
Sampl Ing/
Clock
C&SO
tf> 2-7
O0/*-/ f£
/ o'-t/-D
//) y <~
/^ ~*>n
tl> V
IT, / ^
i <-f / c
I $ l*^
Id, I 5
n K
/fl/s
/
y^,6
^ x>
t~i*SL
9i>^
1 e^>
s', 3
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3.5
2 ,f2
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Draft
(In
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rt >"*,(,
tMt-
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Comments
Ki/\:.//rt-r- \,tf li'f- -c,,r i-~Uvy .
ff.O/, ^ -J ^.;"!«< /Xf ^".-,4 I"., ifi.'<;.>.-(7
'o'l.1?^- -fv^-ib.^ (^->c.,(;
vj *
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)
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Prn
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nternal
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;/(>(.>
let1.
A>9/
^'7cl
ci~f>
ffi^y
93^-
7y
A'2"7
/o3l
<;<^X
7/£i
ft.."*
W
^i
Surface Temp.
Top
Rear
Bottom
3-0
~?C 7.
1^.°)
f/'ZO
V/ "L
V / 3
"? V2.
•2;/ 5
"5/9
"? S^c>
T?7o
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^^2-
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^ .^ ^
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Right
Left
Stack
Temp .
V' u/
?9*7
5*71
V ?c$
<•//<•
277
?.c//
^(•> 6
'.i/'S"
7 ^2^'
Z"7
S C
55 "3
^o
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b V
9 ^>
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^•9
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Room.
Temp.
6--4_
d>"2_
<^?'
//y
~7o
& *5
^" ^~
^ T^
<£ <"
?.9
^^
9?
S:
(j, '<^
-------
I
ENGINEERING-SCIENCE, INC.
Wood Heater />/<
Date //- 3d o -5-H
ling
15
SAMPLING DATA
Sampling Location C-/>i*s7e
Sample Type
Run Number ~
Operator
Start Time
Stop Time
Probe Length and Type /y
n 9
id H-
Pi tot Tube Coefficient
Assumed Moisture
Sample Uox Number
Meier Box Number/_
Meter
H
_/£.
A/ A
Pretest Leak Rate
Post Test Leak Rate
Head and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
time.min Clock)
U /Z/f
t<± 1o
t/tf Crf^
60 1 ^ / *>
-7 f -j_,
c)o . <-j ^
A:><5" erf.'
rzo ILI /c
)$*> ~\O
I Gf> V*»
/ /'. I c> J*)
/y^ 3.0
?y<3 L/'>
z?*9 ^'
2^ /^0 ff,
2 C^7 3^
2 To V^
•25?^ <5t>
^^* 1 7 /^7
"^/ ^7 ~*>c ''
-3,-y^ ^-\C,
*? V ^ ^ -^
3^£3 / 2 / 5
Gas Meter
Readl ng
(v ) ft3
*> > 1 > & 1 1
SH/t S
/ClTr •£*
,
(lll^-'Ll
(?-)<-/ C->
-7^^* r
736- V
Velocity
Head
( Ps). I"-
toyif
* c>v<-
£' *•! C^
4 O ^ J
- r/^o
a 0V?
o pTo
A Cl C) fl
* o vc
^ <^> yc
• * r>V^~
< c1 V (•'
, <•, iy ^,
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• n *•/ C-
a 0 •-/ ^
«<9 V7
* e> H 7
a 0Y"?
. o1-/-?
Orifice
Di ffere
( H), in
Desired
ressure
•ntial
H20
Actual
, 6 7
'67
- If 1
(f 7
«. ^ 7
a (f 7
- ^ 7
a /'• 7
/ <<7 7
^^ *?
• c. 7
« ^ 7
• 6 7
» <£ 7
• u>~/
.('7
.^ 7
f f" 7
,,•-;
/- "7
, 6 1
-67
.6, "J
TEMPERATURES
Di lution
Tunnel
'
Meter
In
(g ~z
Filter
70
Fmpinger
*? ~i- ~
7V
V7
6*? V 'b-'
77 ^^
77- :>-S
S 7 ^*v
7^ ^ -;-
Pump
Vacuum
1n. Hg
7
^
•£_
*
*-
7
i—
Flue Draft
in. H20
I
OJ
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
AJL
Hood lleater_
Date )>- ?
/
Sampling Location_
Sample Type *yC^-
Itun Number X2 - "•?
n i ~£3 ^T~
Operator /i^ , fc
//
"\^ Clock Time
Sampllngxf 24-hr
time, min^vClock)
^Z~a — <^-Si/5_
T75- • 3o
.3?o ^5-
V»5 ^
v^; V5
y^-5" or.
V«o -2^» ^
^"?<" 3^'
S/tf <-y;
^Z^ co
5~v^ *7.//^
5^ 3^
^7o VS
5-7 i Z/V7
Gas Meter
Readi nn
-7*4 >
^If^
.&>-?
• <•-)
.6-?
• CO
• 6 -)
.1 -}
.(,-)
. (, 7
.t ~?
TfiMPERATURES
i)i hit ion
Tunnel
Meter
In
T^.
%/
S3
^ Z
-
Muter
Out
S
-------
FUEL MEASUREMENTS
Date //- ^v-'-oy w00d Heater Manufacturer 5
Project No. Wood* Heater Model A // - /
Run No. "Tl-^\- /
Circle One: Pretest Fuel • Test Fuel
Fuel Type and Amount 2x4 ~2- 4x4_2n__ I*4
Ideal Load Weight ; .Actual Load Weight ~
Fuel Piece Length / -7 .
Moisture Meter Calibration 12;T^ "^ 225 "Ht. ,
Moisture Content-(Meter - Dry Basis)- Co»vK7i
-------
TEST
B-3-2
-------
Method 56 Proportionality Rate. Flou Rate,
Burn Rate, arid Sample Volume Calculations
I
NJ
I
Stv manu: SIEET HOME
Model no: flK-18
Lab name: ES/CB
1st date: 12-2-89
Run no : B-3-2
1st time
(rain): 616.00
Chrg ut
(Ib uet):
run
time
(run)
0
60
120
180
243
300
360
120
480
5-10
600
616
31
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
.90
dp
H20)
H20)
045
015
015
015
015
015
015
015
016
015
015
011
Units l=metric,
2=English:
Y, DGH:
Pi tot co:
Gas MU :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Mood moist ('/. uet):
tunnel
temp
(C.F)
89
96
98
97
1 00
95
96
97
98
1 02
1 06
1 07
DGM
rdg
(m3,ft3)
816.512
876.900
907.600
938.500
969.100
1000.200
1031.100
1062.300
1093.500
1121.600
1 155.900
1180.068
Burn
DGM
temp
(C.F)
71
79
85
87
86
86
85
83
83
85
83
83
2
1.009
0.99
28.56
21.%
0. 1963
18.18
Samp vol
(sm3,scf)
210.613
Flou rate
(dsm3mpdscfm)
132.88
rate (dry kg/hr):
DGM dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(m/nin)
(ft/min)
1007.86
1011.26
1016.08
1015.17
1017.90
1013.35
1011.26
1015.17
1027.31
1019.72
1023.31 ,
1012.80
I.IO
PR
m
100.7
lOO.O
99.2
99.1
98. 1
99. 1
I00.3
100.8
IOO.O
I01.7
I02.6
dDGM
vol std
(m3,ft3)
22.118
22.312
22.210
22.129
22.098
22. 170
22.126
22.509
22.137
22.198
17.136
85.19
17.610
160.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1016.11 98.12 83.00
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED ' "£_ ~L--Q°\.
DATE RETRIEVED
TEST LOCATION CL-T^
SAMPLER SN# ^\^o2-'^>C/
(HG BAROMETER UNCORRECTED)
PRETEST B.P ZZ.O 1.
[ PROBE O , ^
LINE •
CONDENSATE '^ .- ^
FILTER* 1 £?,<:?
FILTER* 2 — O fi H
TOTAL (MG) 1 r C
TEMP. /9 (C)
HG)
TEMP. "L
SAMPLE FLOW RATE PRETEST
ROTMETER (0~/ -(ML MIN) U'U
POSTTEST
ROTAMETER S'9
-(ML MIN)
PRETEST LEAK CHECK
START 6, | (IN H20) FINAL 5C\ (IN H20) LEAK RATE 0(
POSTTEST LEAK CHECK
"i-
H20 MIN)
START /. / (IN H20) FINAL Aiy^/ (IN H2) LEAK RATE g .- "L ( IN H20 MIN)
POSTTEST GAS ANALYSIS
CQ2(Z)
RUN COMMENTS:
^ i-j<"
(V Z-
Hr;*-~ ipofi^cy c.-'V
UV
co(Z)
/o.f
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
M i N ..
DELTA .
PROBgt-FITTINS
SAMPLE LINE
CONNECTOR
1.1VX?
I-B-3-2-2
-------
CLIENT L_
ES PROJECT RD )2~3
PARTICULATE WEIGHTS SUMMARY Page of
RUN No.^ffi'-#--'3-Z Placed in Dessicator: Date/Time |? -^-^9
STOVE MODEL Mo.
POSTEST
••
1 WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
/*••* (55* •!./«•«;
{2~*(&i /r- /
ROOM CONDITIONS
RELATIVE
HUMIDITY
/2^7/
/(7 ®-?/
BAROMTRC
PRESSURE
1-/,ct
Z/, %
Initials
A1C/?
/»ctf
I
co
I
(A)
.(B)
I
CO
-------
/I/
,
CLIENT
PARTICIPATE WEIGHTS SUMMARY
RUII \\Q.vrJ ' 15' 5" <- Placed in Dess ica Lor:
of.
-l-.R /Tima
-V-
ES PROJECT P/)
STOVE MODEL No. //A" ' Q
POSTEST
Acetone Lot \\__VJ_J-
Acetone Sample Volume /?
,-70
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
,2-*-<^//o*
ll't&li/S
thWl
BEAKER It
/?-/<93
/ x * £3 £* o -•*
^ A f K* 1
7x— / 1 ~t
t> . 6?° / '—
. CXiXe0!
CALIBRATION WT
WT AMOUNT
PRE WT
S O J ' r&Cl f
^a.a t~o 1
—
POST WT
•Cx, /
J° • Ot)f 1
6 0. CHOO
ROOM CONDITIONS
RELATIVE
HUMIDITY
lo®-)t '
M© 7.
BAROHTRC
PRESSURE
z// s»
4/, &
Initials
/**/(
I
ft* C <0
I
CO
I
CO
I
NJ
I
(BLANK CONC.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICIPATE CATCH (A-Hi+C)
V/7
-------
PARTICULATE WlilGIITS SUMMARY
Page.
of.
W
I
CO
I
CLIENT /"/Vy RUN No. /?" 3 2
ES PROJECT /{P /2"3 STOVE HODEL No.
POSTEST
Placed in Dessicator: Date/Timo_L^—t^=.
- IV
Acetone Lot II /? ^ Z-
Acetone Sample Voliuna / /
-.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
/2-yfe>///o
K- Jfe5*3zo
/Ay-51
WEAKER II
/?- 'oT-
s^.^/vv
c? / *^ y ^/ x
V f + J f f (0
*/* 3/^p
^,^5
$a,crrnl/
POST WT
5o . £>c>o /
jSb.^^rS
ROOM COM D IT IONS
RELATIVE
HUMIDITY
/&&?/
(*t@7/
BAROMTRC
PRESSURE
I/. <%
i-/, s?
Initials
w*A'
f*cl<>
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICIPATE CATCH
-------
CLIENT
PARTICDLATE WEIGHTS SUMMARY Patje_ .of
RUN No. /?'3-^ Placed in Dessicator: Date/Time /2-
ES PROJECT $. D IT- 3 STOVE MODEL Ho.
POSTEST
••
• NT 1
WT 2
HT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
/Z-'J-^z/'io
11 --y (&/v2&
II- ? - S <7
FRONT
FTf.TKR II
ftE-'l'
• 7/02.
<• 7/o ^)
r 7 1 toC
* ^793
* r 3^-7
BACK
FILTER II
fl£-ni.
- CS7T
>6syj_
- 6«V2
- 6 S 2 ?
• c c / ^
CALIBRATION WT.
WT A HOD NT =
PRE HT
- v^?-?^
,- fTtfo /
POST WT
,. ^<-^7^
' 5"<'6 /
ROOM CONDITIONS
RELATIVE
HUMIDITY
,1(9-},
/c&~>!
BAROMTRC
PRESSURE
•z./. «/
-?/, y
Initials
(
^Hd-x?
^*<-^
OJ
(A)
(D)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f lS-3-
ES Project I
Wood Heater Model Al<-'
Operators 00> ^
. .\iHcJK
TEST RUN INFORMATION
Attempted Burn Rate (-Kg/hr) Qfj Secondary Air Setting
Achieved Burn Rate (Kg/hr} (.C^ICfl Thermostat Setting
Primary Air Setting May Other Settings.
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (I)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Pretest
•z./.'/o
&3
e
o
f& 6/ia U
^70
&OOO
Post Test
•L/.9C -
7o '
^
o
10 *t //r> . f>
"^^V
TEST FUEL DATA
Fuel Charge Rajige Wt./Z-6 to /'
Cill^ • ,•-
Actual Fuel Charge Wt. ?:> I. /
Z..
Coal Bed Range Wt. 2- b to
Actual Coal Bed Wt.
Fuel H20i Dry l_
Fuel: Dry Kg
Wet f.
1 . 1 '/ k
By-pass
Door _
Veloci ty Traverse
LOAD ING/TEST START OPERATIONS
Air Setti ngs
Comments
IP
A 1
p Temp
76- B 1 WfO
Ave. p
0-04-7
Pi tot Leak Check
?y 4 .047
I-B-3-2-7
-------
ENGINEERING-SCIENCE, INC.
ClUnt. tFyT Hun I
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Cliarye
Paye I of
Date \2--1-- &1} Wood Heater Model /
ES Projec. I
M
1
W
1
u>
1
to
1
CO
Time
Sampling/
Clock
OTZJ
A -T L^ C.
(} *3C C)
<3 83^>
°£W S
C>cif>C>
OHl C^
6c|3i>
h */*/S
/GOO
lloo
i2oo
/"^o O
iy e*o
)c> oo
/£• f^>
i 1 te.
I"! *» (e
V *7 fi-T>
7 0-vrj
~?c> VS*
Test
Fuel
Vt.
(Ibs^
LI.LI
0~l
I- &
7. °?
fy°l
(,t.C\
4.O
^> Vi
>. 1
!2.Gj
^,1
V-0
. z.
£}*&
*? s(j
-$,o
/. T
OfCJ
1.7
/. z.
Flue
Draft
(In
.6^2-
. 032.
D'Vi-
o^t->
6 3 6
07, ft
0*315
£>*•/ 2
Ol/7^
ovt
0^7
ol?_O Operators MlM-l
\k
-/ 8 Coal Ued "2 . 6?
\a ^
Comments
((*,/lcJ/,> y } *!•£- \>\
/•>f< -Ws'V ^v) u* U^.i^o. (•*
^L x/f>X -**-"-*-oV-*j~ <'-p'..ti'As/~ i'5"Of'-J. (' '<;oV ^ (•• ••••.\\lv
T^? ?. '^^Vil'7^'^- 'A'.r'r <^\ |'<--0
l/
1
Ciitnl.yst Temp
Prr
SS^-/
?i/ "
2i"7
c'/U
C-^tiJ
\*>7_
V^ c^
7V/
t} L/{_ /
/V "S
soy
sv^
^
T^f
it
nternal
Post
f.V-S
/fc.l
1 /<->
L/QlJ
i^i G
0.1 -)
6C'|
6^>i
'7S
t'l'r-
"fj
9v> f-.
9V/,
O^f^-
~)'%>
~7f.~^
*)'•<•
??Y
/••L/cr
Surface Temp.
Top
—
Rear
bottom
/ "7 ^
/A 7
? <_'< <-/
~\l I
~*>f& 7_
?,V 8
^' ?
34 o
^,9/
^fi'l
V5 "^
v^1 y
396
V/9
VZ £-
Z-T—
_l/'±L
~2>'ri *>
~3 & 7
Right
Left
Stack
Temp .
2. 3
i'&U'
3vS
3*3 1
"3S /
•39 /
37 /
•^77
39o
-57'
"2,
"^z 5
? ^ V
^ ,S T
Dll .
Tun .
Temp .
76
-7T
7S'
So
ff 3
5i4-
e#
ti"x
Q c/
'T('->
?8
97
/^-z?
9 T
"? &
<9 7
9 S'
<9 S'
/jj • ^
/(-. c
Room.
Temp .
(f~j
<""?'
rj'c^'
ScT'
fi^
«r **
^
67
(5 \
C~~7
&•&
£.<-'/
& ef
6 7
6> *?
7o
~? /
7o
//. V
/ ,.
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date 1-7
SAMPLING1 DATA
B
Sampling Location
Sample Type
Run Number "fo.
Operator
Start Time
Stop Time
Ambient Temperature^
Barometric Pressure_
Static Pressure, (P^
Filter Number(s)
Meter
AK. iiv
Probe Length and Type_
Pi tot Tube Coefficient_
Assumed Moisture */
Sample Uox Number
Mater Box Number "/>
Meter H
• "> ?
Pretest Leak Rate ,
Post Test Leak Rate
!r> er. 10
Read and Record All Data Every (ft) Minutes
Clock Time
Sampling (24-hr
time.min Clock)
(s 1 & & £^
1*5
*^?o
1*7
(f>O I /OO '
"7S
(•10
loc-,
i i<-> (-£.&o
l.ic>
/fiCi
A?S
/'P)O / T.OO
/'1fS
2-/O
2.2-3
1HQ /«-/Co
1/SS
170
^OO /'iCo
• .q
r^c)
'WS
"V; ftft't'
Gas Meter
Readi ng
(vm) ft3
8~7 b • ^[
cfil. G
c/ vc;'. S
9 ^-9. '/
1 Ci-C'U • £_
/ol/./
Veloci ty
Mead
( PS), ^.
H20
-OV^,
• O'YS
D *-/^
fc>«V.^)
• ^''c ^
i v~lLt
. <^-l S
. OS'S
. 6 L/ S
• ° V5
OH 'o
, t>c^
,oS '3
.OM'5
°'-("5
r 0 V T
^ o '/ 5
, o V r)
*e)1 <^
^ c.' '/ <7
, o M S'
„ n H ^
o (s>!~7
.([-,— 7
. 0-7
*<' "1
•6l7
.07
c.-~/
.0-;
fo-j
.tc"l
* <^-/
At"]
.L.-I
, (.. 7
!<"• ")
.6'-;
, ^.' 7
, ^r 7
TEMPERATURES
Di lution
Tunnel
.
Meter
In
~~7<~j
i.9 •:^-
^r/
*-». >
S S '
"?> 7
_. ^7-
Meter
Out
1 1
-7V
Ct
<;, ^,
-sT
Filter
•
Impinger
4_\3 •S'S" •
76' 5 ^
.^0
'; A
.^/
•? 7
*.-<->•
7-
•^
.._"?- ... _ .
Flue Draft
in. H20
I
OJ
I
N>
I
\0
-------
>3
SAMPLING DATA (cont.;
Vlood lleater
ENGINEERING-SCIENCE, INC.
•
Date ) 2. -7. - s 1
Sampl i
Sampl e
ncj Location cv f c P~t" r/ /^^-irtT^
Typ,e ^C
„ ^
\
Run Number 13- 5-7
Operator /-^x e /\ t^j #-
M '
tu
I
UJ
I
N>
1
X^ Clock Time
Sampl 1 ng\(24-hr
time, min^xf]0ck)
^2fO — ' —— ^6_f£;
~\ 7T • / •?
"^ 9 o "j &
<-/(>$ t/<;
VZ^ / "7 c>zTJ
V 34" / <•
V £0 ^tf
*/£<5" i-/^
V 3<9
•5"^ £" • i/^
^" y^> /
^5 ~t,(,
S^c; V5
fatt '? ^<-^
fr/c yf
ff'i^ *-/<
/^V6 lot 9
// {?r> .cV-Si
Velocity
Head
(al's) in.
^ <:••-/ 5
. o v T
f <^- V 6
v r<<-/ ^
M & V ^T
aO*/*>
« «•/ 5"
, r, V"T
f fj'/(-
-' O V T
p ^.. (./ ^
. ^ V 5
r< VL/
^ Ci H H
' /-.(-/I-/
Ori f ice 'ressure
Oi fferential
(All), -in. ll?0
Uesi red
Actual
. (n 1
. (n 1
«, 6 7
. 7
x 6 7
.• ^ 7
> /- ~~>
-/- "7
. ^ 7
•
V><^
-------
B-'V
FUEL MEASUREMENTS
Date ( 6. -~L
Project No. f(
Run No. Sfe
Wood Heater Manufacturer
Hoocf Heater Model At/-!
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight •_
Fuel Piece Length [_
4x4 ""?—
1x4
.Actual Load Weiaht
Moisture Meter Calibration 12%
221
Piecs No.
1 ?Ie H
2
3
4
5
6
8
9
10
ll
12
13
14
15
16
17
18
19
20
Moisture Content- (Meter - Dry Basis)- Coiv«7td.
Readings Average
1HJ_ ZM.I.
UL- 2— iZl2-
2.H.Z zs& z/.y
13,2 1.1.0 23T,
Z3,^
2^-5 say 25,7
Overall Fuel Moisture Average
I-B-3-2-11
-------
TEST
B-3-3
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and San.ple Volume Calculations
I
W
I
u>
I
OJ
I
Stv manu: SHEET HOME
Model no: fK-18
Lab name: ES/CB
Tst date: 12-3-89
Run no : B-3-3
Tst time
(min): 537.00
Chrg ut
(Ib uet): 27.50
run
time
(iiiin)
0
60
120
180
240
300
360
420
480
540
vel dp
(mm H20)
(in.H20)
0.042
0.043
0.044
0.044
0.045
0.043
0.044
0.045
0.044
0.045
Units 1-metric,
2=English:
Y, DGI1:
Pi tot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Uood moist (?. uet):
Burn
tunnel
temp
(C.F)
91
99
%
9?
94
%
94
%
98
92
OGM
rdg
(m3,ft3)
160.701
210.500
241.100
271.800
302.400
333. 100
363.800
394.600
425.700
455.380
OGM
temp
(C,F)
73
81
86
88
86
86
86
86
86
84
Samp vol
2 (s«,3,scf)
1.009 197.897
0.99
28.56 Flou rate
21.98 (dsm3ft,dscfm)
0.1963 131.66
17.20
rate (drg kg/hr): 1.15
OGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
M20)
670
670
670
670
670
670
670
670
670
670
vel
(m/min)
(ft/«in)
975.01
993.69
1002.47
1003.37
1011.98
991.02
1000.67
1013.80
1004.27
1010.15
PR
(.7.)
102.
101.
99.
98.
98.
100.
100.
100.
95.
4
1
8
5
7
4
2
2
5
dOGM
vol std
(m3,ft3)
21.921
22.178
22.046
21.894
22.046
22.046
22. 1 18
22.334
21.314
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1000.64 95.30 84.20
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED ( 2. 3" C°f
DATE RETRIEVED
TEST -LOCATION C. "[S
SAMPLER SN;/ ~lt-f fd'~^
(HG BAROMETER UNCORRECTED)
PRETEST B.P Z.Z./O (IN HG)
TANK Z.Z-.C5 ( — IN HG)
TORR ABSOLUTE ^2 i I . 1
POSTTEST B.P. 11 >OT_ (IN
TANK/ 2 « 7*3 ( — IN HG)
TORR ABSOLUTE Z?^i w^/
WEIGHT GAINS
PROBE £ . -^
LINE '
CONDENSATE 9,6
FILTER)? 1 O . A
FILTER// 2 — O , <^
TOTAL (MG) °l „ "2,
TEMP. 3D (C)
HG)
TEMP. 7. %" (C)
RUN)? ,S 3 ~ ^_
-7 :, LI U.-
STOVE ID Ak-l&
WOOD SPECIES U-^> TiT
WOOD MOISTURE (Z DRY) ZO
TTrt^ rtT •T.Tm /IT
WOOD CONSUMED (LB) 11, S (
SAMPLE FLOW RATE PRETEST
ROT3HETER (j^ -(ML MIN)
POSTTEST
ROTAMETER £ C- -(ML MIN)
1
,7CS
KG)'!''
6/.o
PRETEST LEAK CHECK
START 5.6 (IN H30) FINALj£6 _(IN H20) LEAK RATE Q. 0 (IN H20 MIN)
POSTTEST LEAK CHECK
START j". 3 (IN H20) FINAL_f. 1 (IN H2) LEAK RATE<^ • & (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
C02(Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST + MIN.
PROEE-t-FITTIMG
SAMPLE LIME
CONNECTOR
MIN.
MIN. + MIN.. DELTh
I-B-3-3-2
-------
Page
of
CLIENT A
ES PROJECT /?/9
PARTICIPATE WEIGHTS SUMMARY
[)fir
RUH Ho.-#"?-'3» Placed in Dessicator: Date/Time /Z-?-Sf
i
STOVE MODEL No. /i] R~
POSTEST
1
1 HT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
^—*
/ 2- */&/*<;*
11-tfQ liH^
It- 1 8 c?
FRONT
mr.TKn n
5^'-/^3
* 120-7
t/2.o5
^ZoO
BACK
FTt.TKR II
SAZ-M
./Zv*
>/i~<*/
. 1 1 <-, /
- u<-t
-.0005
CALIBRATIOM WT.
WT AMOUNT =
PRE WT
, £]esO /
. $**/
POST WT
c 5^7/
j"&-J&
BAROMTRC
PRESSURE
T. /. ?
•2-/,^
Initials
I
McJ
tne/?
w
I
OJ
I
U)
(A) (D)
)
-------
V.
29
\
co
Page.
o-C.
CLIENT
ES PROJECT /*/? /*Z
PARTICULATE HEIGHTS SUMMARY
RUN \\o.\iPI- B' ?"3 Placed in Dess icator: Date/Time
STOVE MODEL No.
POSTEST
Z ^
Acetone Lot ll
Acetone Sample Volume _ /
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
WT 1
WT 2 .
WT 3
HT 4 .
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
ll-'i^ //^5
i?-^<9^1/5
y/ - v - s •?
HEAKKR II
A/^y
8^ , Si^ 9 5-
^o. £7^,
«?«-?} 7 ^y
. D0^(^
CALIBRATION WT
WT AMOUNT -
PRE WT
£o , OS* /
"CO. 0-£r* /
POST WT
*)£>,c>etj
<>o. e^aye)
ROOM CONDITIONS
RELATIVE
HUMIDITY
/*&7/
/*&->!
BAROMTRC
PRESSURE
1 1 • "6
\-t. *
Initials
M^/3
£+.c4.
-JJ. / . ^ f\ . 1 11-, iiif . 1 / . -7 o s .
(C)
TOTAL PART1CULATE CATCH (A-i-BiC) =
7.3
7. 3
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page - of
HUH No. $~ $ 7> Placed in Dess icator: Date/Time. Il~y-
ES PROJECT f\0 12 **> STOVE MODEL Mo. tf'/< ^
POSTEST
Acetone Lot ll 7 *• 4* ^
Acetone Sample Volume.
° ( c
7^
• 76
7
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
i-
TARE WT
NET
DATE /TIME
l^f& /.lie.
1 1- H<& I-^LO
//-v-^,
HEAKER II
7£* ?:^^?
^
-------
CLIENT L P fl
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No. 13 ~ 3 - ~3 Placed in Dessicator: Date/Time_/JjJL
)?-J>
STOVE MODEL Ho.
POSTEST
1 WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/2-V 6? /<.-»-.Z5
/1-ffe? Z/f?
//- ? - ^ r?
FRONT
FILTER II
/9f-/97
a 1 i&~)
">.' / T>
I /! / if
• Tol
,-7/oV
*6> ^o3
,6•bQ^
BACK
FILTER II
/?f- /9 ^
'5
»
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' " Run /
Project f
Wood Heater Model
Operators lAJfrn
TEST RUN INFORMATION
Attempted Burn Rate (K-gfhr-)- *> Comments^
Temp
A 1
2!L
8Q
86
B 1 ,0
3
4
Ave.
Pi tot Leak Check
I-B-3-3-7
-------
ENGINEERING-SCIENCE, INC.
Client |^ PA Hun
Date /2_-1>-@cf Hood Heater Model /\i('/ o
ES Projec. f
M
1
W
1
CO
1
oo
Time
Sanipl Ing/
Clock
Ofc.i-7
OS"-/1^
c^-\'^c)
Cy-\ H ^
/e>oo
to
!<> / f
(I/ S
;?./ s
/TC5
/^-/|
b< p^
"\ * (f
1 . Z
/«,"?
flijo
Flue
Draft
(In
orsft
o 3 '7
*o vf?
,o y?
C-/Z.
f.VZ.
ol^,
c-H'i-
4><^VO
/ £> ^£-
t>0L/^i
tC^>^
/^D/i'^i Operators tO/-/M ^/^
Comments
K-Af^v^c/ "Hfp I ,~\~
1 ;,// z.,6 x] ^-16 " f'.v - /^ '.f
• '
6''V? f^U-Cit '?,,- J ^.
,
3" '/fiy? 7 0 . 1 > J 1 f •!<> < '•:•< /
• ivf c,,^u^ A-,-.j,.^ /Z./ a/ /y/i?
CryH-^ S. O ' '/*• ' V
C a t a
Pro ||
t/y'o
^,1*-!
^/c
9 ?t
rV/
A-^ 7
P6?;
3i 2 7
?!"}?>
^7"^
^ *s o
Cj /, C-J1
7 I/
HOOD IIEATEIl CEIITIFICATI OH TEST
TEMPEUATUUE AND FUEL CONSUHI'TIOM DATA SHEET
Test Fuel Charge /?.
Coal Oed "3
Paye / of
Catalyst Tcnp
Pf; llnlernal
6'Vo
•^,:iv
^;
9?^.
'rV/
"4-'' 7
f-^?i
r'v77
?:^^
^7'^
^^0
s^
'?!/
Post
6,V
«7V
/,•"/
r^
;67?
7V 7
W^
(£4
/72-
/<>>-)
•hl3
V/7
-»,e.'/
•v/-\
V^>T
V3S
V? •?
74. y
Ilight
Left
Stack
Temp .
T,#
^/
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date 7
SAMPLING DATA
U
(. i
Sampling Location
Sample Type
Start Time
Stop Time
Run Number /^-
Operator
Ambient Temperature (^>
Barometric Pressure ~i.7. ,c
Static Pressure, (Ps)
Filter Number(s)
Meter /. ^ 9
Probe Length and Type /y — (7/>;
Pi tot Tube Coefficient „ ft
Meter H
Pretest Leak Rate 0-OC.o
Post Test Leak Rate a >M ^
/„ £• <,-£,
/ Z/v> /7./"7
/ If -V'
/ Si? V"^
J ^^" ^y
/^o /~$/^
/<9 /*T
1? < <5tJ
2 Vo / V /"^
-7 <<^- -5^,
? 7^ *>">
-^ ,Y^
'^ /^•/'T
Gas Meter
Reading
(vm) ft3
? /^i S
Z-V/. 1
-^^/T~^-
,
zrii.X
'tfOZ.t-/
**
^33 [
i
'tih'2> .^
Veloci ty
Head
H^O*
,. C>L/T.
c><-/ 1—
a (. •> V "•?
. c> y "i
i O<-y "S
. i-.-vY
6VS
. o'-'fH
. C>'f ^
o vv
, 61 -V ^
0 •-/ -^'
,0'/,S
. CJ'-/ ".->
c ' H (/
• OS "\
(j*-/ 3.
.O1-/ ^
, "V-/
.6 Vi
, 0 L/V
.( ^ V V
Orifice 'ressure
Di fferential
( H), in. II20
Desired
Actual
.C.-7
, t- 7
/ — 7
. 1 .- /
,0-7
-67
, (^,— /
•G 7
.07
•C-7
• &-7
•d'7
.6- V
,67
.•-Y7
, C, 7
,GI 7
( ,—y
• £,'"7
•C 7
'. ""7
• £ 7
- /; ")
TEMPERATURES
Di lution
Tunnel
i
Meter
In
-7V
0 <-/
fl&
i"'-V
(.WI c '
fc--h
S 1
Meter
Out
7-*,
i ;' /
\_J/
,*•-/ <1'<".-
7U- --> V
77 :;/
.So ^ c:
Pump
Vacuum
In. Hg
2
j>
7>
^
— >
7r
p
Flue Draft
in. H20
oa
I
u>
I
U)
I
v£>
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (con I.)
Hood Healer /) /< -
Date y 2 - T - S *?
? -
- 3-3
Samp li'mj Location C ^ f f, V f <:/
Sample Type ^"tf- /^oc /<
Run Number
Ope r a to r /-
f ys>'/<
V cl $ ~\<-^
1JO i-l *j
<;?<; tro
Ttt?$37 (ci/5
Gas Meter
Rcadi nq
(Vm) ^
T) y. o
^-/ 2 S . 7
_ V5"S,~3*c
Velocity
Head
(A!'S) in.
11^0
a <5 V^"
. S'
S?
<5iS
-
Meter
Out
-------
1) "3 3
FUEL MEASUREMENTS
Date /^- :?-£=->/ Wood Heater Manufacturer Si_JJ
Project No. Wood-Heater Model f\\/-/ <*=>
Run No. ~g_ %. - -v
Circle One: Pretest Fuel • 1^t_F\ts\
Fuel Type and Amount 2x4 ~2L- 4x4 "Z_ 1x4
Ideal Load Weight ; .Actual Load Weight
Fuel Piece Length / £3 '
Moisture Meter Calibration 12; T£ 6 22' Z-f- 5
*J»vd r*~,s.°F .
Moisture Content-(Meter - Dry Basis)-Cor"'1£c'^. I r I ~\
7' /*7 -di1 f\j (,' I
l*^ '' *^^—^—
13
14
15
16
17
18
19
20
2.2.0
4
5
8 /1_±
10 Ml ^W ZY.
Overall Fuel Moisture Average Z.O -~7 >"
I-B-3-3-11
-------
TEST
B-3-4
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, arid Sample Volume Calculations
to
I
Co
I
Stv manu: SMEET HOME
Model no: fiK-18
Lab name: ES/CB
1st date: 12-4-89
Run no : B-3-4
Tst time
(min): 622.00
Chrg ut
(Ib uet): 36.20
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
622
vel dp
(mm H20)
(in.H20)
0.044
0.043
0.044
0.044
0.044
0.044
0.044
0.045
0.045
0.043
0.043
0.043
Units l=metric,
2-English:
Y, OGM:
Pilot co:
Gas Mil :
Pb (mm, in. Hg):
Tunnel area (m2,ft2):
Hood moist ('/. uet):
Burn
tunnel
temp
(C,F)
93
98
99
98
95
103
103
93
91
112
115
112
DGM
rdg
(n,3,ft3)
456.112
486.300
517.100
548.000
578.800
609.900
641.000
672.200
703. MO
734. 700
765.000
777.456
DGM
temp
(C.F)
73
80
66
38
8?
88
91
87
80
86
88
88
Samp vol
2 ( s,i,3, scF)
1.009 229.417
0.99
28.56 Flou rate
21.80 (dsmSro.dscfm)
0.1963 130.35
16.67
rate (dry kg/hr): 1.32
DGM dH
(mm H20)
(in.H20)
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
0.670
vel
(m/nlin)
(ft/min)
1003.88
996.89
1009.31
1008.41
1005.70
1012.92
1012.92
1015.23
1013.39
1009.31
1011.96
1009.31
PR
(.'/.)
99.
101.
98.
1
5
1
9
97.8
100.
99.
97.
98.
103.
99.
110.
6
7
1
7
2
1
9
8
85.49
17.640
460.00
1850.00
dOGM
vol
(m3,
22.
22.
22.
21.
22.
22.
22.
22.
22.
21.
std
ft3)
026
181
009
857
111
070
021
253
469
501
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1009.10 101.00 85.17
8.839
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IM-SITU TEST METHOD
DATE DEPLOYED
DATE RETRIEVED
TEST LOCATION
SAMPLER SN#
(HG BAROMETER
PRETEST B.P Z/
TANK Z 1 . 3 0
TORR ABSOLUTE
ll-'i-gl
CTb
^2.3H
UNCORRECTED)
,^3 (IN HG)
(—IN HG)
,70
POSTTEST B.P. T_ /,^q (IN
TANK //,*/1 (Mtil.)
STOVE ID AkM 6
WOOD SPECIES J\ f-~i.~
WOOD MOISTURE (2 DRY) 2-'^ 1
WOOD MOISTURE (" WET)
WOOD CONSUMED (LB)>i,l (KG)/'i'.V
SAMPLE FLOW RATE PRETEST
ROTSJfETER & 1 -(ML HIM) 6/.C
POSTTEST '
ROTAMETER 6- C; -(ML MIM)
PRETEST LEAK CHECK
START $-H (IN H30) FINAL 5.O (IN H20) LEAK RATE i V (IN H20 MIN)
POSTTEST LEAK CHECK
START ?. / (IM H20) FINAL*?.g (IN H2) LEAK RATE £>.
-------
PARTICULAR WEIGHTS SUMMARY
Pace
of
CLIENT
ES PROJECT
RUN No. UPX- ($~3 V Placed in Dessicaior: Date/Time /2-g-V?
STOVE MODliL Mo. ft l< ~ ' **
POSTEST
v
• WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
n-5$?o3S
/2-4 <2^23o
//- 3-2 *?
FRONT
FTLTRR II
SA O
POST WT
. C^-«» /
e $Cr6 /
ROOM CONDITIONS
RELATIVE
HUMIDITY
l&®tt
;3 ®?&
DAROMTRC
PRESSURE
Initials
t
S*c/t
S*t<-/^
I
Cd
I
OJ
(A)
(B)
-------
I
UJ
I
.CLIENT Z7/7/)
PARTICULATE HEIGHTS SUMMARY
RUN No. {/PI' O'^Y Placed in
Page.
of.
ES PROJECT R f) 17 3 STOVE MODEL No. /)/<-/¥
POSTEST
Acetone Lot ll .9.'^- 2.
Acetone Sample Volume.
•
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
IZ^&i
-------
CLIEHT
/."P/9
PARTICULATE WEIGHTS SUMMARY Patfe of
HUH Ho. fi~ 3~ V Placed in Dessicator: Date/Time / "Z. ~5"-
ES PROJECT /IP / ? 3 STOVE MODEL No. /?' )< -
POSTEST
L3_^tfzo
/v I
Acetone Lot II 9 2^ 6 Z
Acetone Sample Volume
'
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FIHAL WT
TARE WT
NET
DATE /TIME
;i-
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page o£
RUN No. B ~ 3 " V Placed in Dessicator: Date/Time / Z. -5 - * 0 ^(/
ES PROJECT R P - /2 3 STOVE HODEL Ho.
POSTEST
-
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
11-S &i° V$
/2-<-(9c?SV5-
)/- 1 - S3
»7/37
.7/3 7
,-?/ 37
/67^
• 03'7'B:
BACK
Fir.TER II
/)£-2oic/l
to
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' ' •' Run I IS-3-
I
ES Project f R\M
Wood Heater Model
Operators _ ^
~( 8
TEST RUN INFORMATION
Attempted Burn Rate
Secondary Air Setting t\J l\
Achieved Burn Rate (Kg/hr) /, 3lO Thermostat Setting
Other Settings
Primary Air Setting
£> - (i 2 Z. rti'o
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Pretest
?./, 9 -L.
&<-/
/o
o
/C.O///J.CJ
y
Y<^<=>
TEST FUEL DATA
Fuel Charge Range Wt. II. O to 16.
*l- 13.1
Actual Fuel Charge Wt. 36>. 1.
Coal Bed Range Wt. Z..7 to 3,
Actual Coal Bed Wt. ^>- i
Fuel H20J Dry ZQ.
Fuel: Dry Kg
Wet
LOADING/TEST START OPERATIONS
By-pass
-------
3 -
ENGINEERING-SCIENCE, INC.
Client EPA:
HOOD IIEATEIl CEHTIKICAT10H TEST
TEMPERATURE ANU FUEL CONSUMPTION DATA SHEET
Test Fuel Charyc
Page
of
Date l"2--^'Sr( Wood heater Model Ak~/fi Coal Ued 1> . |
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Temp.
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-------
r-*^
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number
Ope r a to r
11- Li -
Start Time
Stop Time
c
\c~j
TV
(Qt-lU
Ambient Temperature
Barometric Pressure
Static Pressure, (P7
Filter Number(s)
Meter If--
K( ( o
T 5
^TO
/OS
( ZO I td O>
/"S5
C56i
/fc^
/fiO ^OC!
rTS
.-^/0
?2S
VS"*
2,70
2C^
,^oO I ^ ^
3""O
3VS
^.-0 /tC:<->
Gas Meter
Reading
(vm) ft3
'-/0^« IS
.
•517, I
.
9V S' /. o
^ 7 S' » ^
(r n 9 ' C/
^Vil_fl
Velocity
Head
H^O*
6,o>'-/V
, o>-/ 6Y
o >-/ 7S
, (j<-i>- (
. &L/ ^>
. ^><~fil
, O '-/'-/
. o <-/Y
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.O'-i'-l
, t><-/ V
' ^ *"/•'/
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.. 0 <•/ V
, <:• vy
„/>'/*/
. ?<•! 0
O Ll '/
a 0 l/ W
. 6VV
., n c/ -?
i. C* *-\ *V
- c' v_y
Orifice Pressure
Differential
( H), in. H?0
Desired
~(t~l
Actual
.67
.67
. <;• "7
• Co -7
0-7
•<• 7
•fr-7
v (j ~l
' {> 1
. /* 7
« ^ 7
. A 7
> ^- 7
• (f 7
. <{,7
j (,• "^
ft "7
• (- ~1
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...*^2_.
TEMPERATURES
Dilution
Tunnel
Meter
In
7 v
£. ^S
tf>iS
s- v
- s ^
°l <>
.. °/ 1
Meter
Out
7 ")
C-c)
'c,l-
•& S'
r? "^
^ *3
- -
Filter
Impinger
70 (< -j •
7fe ^ V
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.;
Hood Heater
Date
/ 2 - V - S 9
Sampling Location <",.
Sample Type 5" ,?r • A' ^'/
,V /I—
-r-
\. Clock Time
Sampling\(24-hr
time, min\Clock)
T2'^ — ' &L2EL
•?75 - ;<
^90 ?6.
V^'T VT
vz^ / -?^>
V?-T )5
V$o It-
V<6^ V<7
t/Sc- /%
(fiS if
(0-1.1, -zoz-i.
Gas Mater
(eadi nq
iynvUtZ_
6,72.1-
->«1.S
-7^.1
765. 0
?7?.VVt
-pt/3
,t>V3
.rt^y^
-C7V^
Ori f ice Pressure
Di f ferential
(All), -in. ll?0
Desired
Actual
„ C..-1
*l. 7
. / 7
, 67
. 6 7
.^7
*(-->
.f, I
./-?
,<-- T
^7
•
•b<-
S Z
% ^
Filter
7 9
^75
8V
fi S
ay
Impinger
Vo
v
7^
2-
•z-
•z_
Flue Draft
in. H20
I
do
I
CO
i
i—•
o
-------
IT.
'**
~B
FUEL MEASUREMENTS
Date /J
Project No.
Run No.
Wood Heater Manufacturer
Wood" Heater Model
A-UT - (
Circle One: Pretest Fuel
Fuel Type and Amount 2x4 <£- 4x4 ~i_ 1x4
Ideal Load Weight
Fuel Piece Length_
Actual Load Weight
Moisture Meter Calibration \2\_
vluvd TV »7 z>. °F
/ -7. • o
225
I. "7
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)—
Readings Average
L /-L- v C~"*'^
-y -"^ k >7«y
Overall Fuel Moisture Average
Zo.O
I-B-3-4-11
-------
APPENDIX J
PROPORTIONALITY DATA AND ALL RAW RUN DATA
FOR THE S-173E TESTS AT CRESTED BUTTE
-------
TEST SERIES
C-l
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv «anu: HftJGH'S PRODUCTS Units l^metric,
Model no: S173E 2=English:
Lab name: ES/CB Y, 0611:
1st date: 11-9-89 Pilot co:
Run no : C-l-1 6as MM :
Tst time Pb (HA, in. Hg):
(•in): 720.00 Tunnel area (n2,Ft2)
Chrg ut Wood moist (?. uet):
(Ib uet): 31.60 Burn
run
time
(mm)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.060
0.050
0.052
0.056
0.046
0.049
0.048
0.046
0.048
0.050
0.050
0.049
0.048
tunnel
temp
(C,F)
58
114
88
85
110
%
90
100
90
82
80
80
75
DGM
rdg
(*3,
179.
209.
240.
272.
303.
334.
366.
397.
429.
460.
491.
523.
554.
ft3)
001
900
800
200
SCO
700
300
700
100
600
800
100
140
DGM
temp
(C.F)
59
86
93
96
99
102
101
100
100
98
96
96
88
Samp vol
2 (smS.scf)
1.046 273.055
0.99
28.56 Flou rate
21.80 (ds«3«.dscf*>
0.1963 140.90
11.43
rate (dry kg/hr): 1.06
DGM dH
(tun
(in.
0.
0.
0.
0.
0.
o!
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
550
550
vel
(•/nin)
(Ft/din)
1134.58
1090.27
1086.39
1124.31
1042.10
1062.26
1045.67
1032.92
1045.67
1059.45
1057.49
1046.86
1031.32
PR
00
103.7
98.0
98.1
98.3
102.5
100.2
103.2
102.8
100.4
98.1
99.0
98.2
dDGM
vol std
U3,ft3)
23.992
22.806
22.882
22.686
22.492
22.659
22.556
22.596
22.668
22.533
22.686
22.498
85.49
17.640
460.00
1850.00
vs/Vi»Ts vs ave tunnel DSH
ave temp ave tenp
(C,F) (C,F)
0.01 1066.10 88.31 93.38
-------
Hethod 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
o
I
to
Stv manu: HflUGH'S PRODUCTS Units l^metric,
Model no: SI73E 2=English:
Lab name: ES/CB V, DGM:
Tst date: 11-10-89 Pitot co:
Run no : C-l-2 Gas M14 :
Tst time Pb Un>( m. Kg):
Uin): 720.00 Tunnel area («2,ft2)
Chrg ut Mood moist (.'/. uet):
(Ib uet): 33.80 Burn
run
tiae
(win)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp tunnel
H20) temp
H20) (C.F)
056
055
051
054
053
056
056
053
056
055
056
054
056
72
103
106
114
%
93
106
103
92
92
88
85
83
DGM
rdg
(m3,ft3)
559.
588.
618.
648.
678.
708.
737.
767.
7%.
825.
855.
885.
914.
289
800
500
300
200
100
600
000
300
600
500
000
804
DGM
temp
(C.F)
69
89
99
99
95
95
92
99
96
98
98
98
95
Sairp vol
2 (s«3,scf)
1.046 258.934
0.99
28.56 Flou rate
21.82 (ds,«3a,dscfa)
0.1963 146.46
14.36
rate (dry kg/hr): 1.09
DGM dH
(»* H20)
(in.H20)
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
vel
(ft/ain)
1110.31
1131.96
1092.92
1132.53
1104.26
1132.01
1145.24
1111.19
1130.99
1120.85
1126.89
1103.55
1121.73
PR
106.
102.
105.
99.
101.
100.
98.
98.
97.
98.
%.
99.
8
1
7
1
8
3
8
3
1
9
5
2
85.49
17.640
460.00
1850.00
dDGM
vol std vs/VaTs vs ave tunnel DGM
(a3,ft3) ave temp ave temp
(C.F) (C,F)
22.502 0.01 1120.34 94.85 94.00
21.821
21.503
21.575
21.730
21.440
21.483
21.142
21.256
21.614
21.324
21.544
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
t-i
I
o
Stv aanu: HflUGH'S PRODUCTS Units l=«etric,
Model no: S173E 2=English:
Lab name: ES/CB Y, DGM:
Tst date: 11-11-89 Pitot co:
Run no : C-l-3 Gas Mil :
Tst time Pb (nun, in. Hg):
(•in): 720.00 Tunnel area (m2,ft2):
Chrg ut Hood moist (2 uet):
(Ib uet): 29.00 Burn
run
time
(win)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp
(•it H20)
(in.H20)
0.054
0.054
0.055
0.055
0.052
0.052
0.054
0.052
0.052
0.052
0.055
0.054
0.055
tunnel
temp
(C,F)
81
97
88
83
86
81
89
119
98
98
93
88
85
DGM
rdg
(m3,
916.
946.
975.
1004.
1034.
1064.
1093.
1122.
1152.
1182.
1211.
1240.
1270.
ft3)
604
000
400
800
400
000
400
900
500
100
700
800
128
DGM
temp
(C.F)
70
88
96
94
96
84
89
93
92
87
87
88
89
Samp vol
2 (s«3,scf)
1.046 259.454
0.99
28.56 Flou rate
21.78 (ds«3n,dscf«)
0.1 %3 145.26
11.77
rate (dry kg/hr): 0.97
OGM dH
(mm
(in
0
0
0
0
0
0
0
0
0
0
0
0
H20)
.H20)
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
0.550
vel
(m/«in)
(ft/ain)
1100.50
1116.65
1117.80
1112.69
1084.91
1079.93
1108.60
1117.21
10%. 76
10%. 76
1122.89
1107.59
1114.74
PR
CO
104.9
98.4
%.o
98.0
99.2
102.6
104.8
99.9
101.9
101.9
97.0
98.4
85.49
17.640
460.00
1850.00
dDGM
vol std
(«3.ft3)
22.331
21.600
21.290
21.512
21.434
21.759
21.634
21.551
21.590
21.787
21.419
21.547
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1105.93 91.23 88.69
-------
Hethod 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
o
Stv nanu:
Hodel no:
Lab name:
Tst date:
Run no :
Tst tine
(»in):
Chrg ut
(Ib uet):
run
tine
(•in)
0
60
120
180
240
300
360
420
480
540
600
660
720
HOUGH'S PRODUCTS Units iUmetric,
S173E 2=English:
ES/CB Y, OGM:
11-12-89 Pilot co:
C-l-4 Gas MW :
Pb («i«,in. Hg):
720.00 Tunnel area U2,Ft2):
Mood ttoist (?. uet):
25.30 Burn
vei dp
(IHI H20)
(in.H20)
0.055
0.055
0.055
0.056
0.056
0.056
0.057
0.058
0.058
0.059
0.058
0.057
0.057
tunnel
temp
(C.F)
86
97
102
93
85
7?
99
95
84
82
79
88
91
DGH
rdg
(m3,ft3)
272.403
301.500
330.700
360.500
390.500
420.500
450.300
479.700
507.800
537.600
567. 300
595.900
625.579
DGH
temp
(C.F)
70
79
86
89
89
86
85
91
87
86
88
87
89
Samp vol
2 (s«3,scf)
1.046 259.855
0.99
28.56 Flou rate
21.70 (dsn3ffl,dscf«)
0.1963 149.50
10.18
rate (dry kg/hr): 0.86
DGH dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
550
550
vel
(in/am)
(ft/min)
1117.82
1129.02
1134.08
1135.14
1126.90
1118.60
1151.43
1157.32
1145.79
1153.50
1140.52
1140.04
1143.16
PR
c/.)
105.
103.
102.
100.
100.
104.
99.
92.
98.
97.
96.
100.
0
5
2
7
0
7
8
0
9
6
3
7
dOGfl
vol std
(.»3, f 13)
22.023
21.732
21.894
21.920
21.920
21.894
21.640
20.458
21.854
21.820
20.936
21.765
85.49
17.640
460.00
1850.00
vs/V«iTs vs ave tunnel DGH
ave temp ave temp
(C,F) (C.F)
0.01 1137.95 89.08 85.54
-------
Method 56 Proportionality Rate,! Flou Rate,
Burn Rate, arid Sample volume Calculations
C-i
I
o
I
i—•
I
Ol
Stv «anu: HflUGH'S PRODUCTS Units l=fl,etric,
Model no: S173E 2=English:
Lab name: ES/CB V, DGM:
1st date: 11-13-89 Pilot co:
Run no : C-l-5 Gas MU :
1st time Pb (mm, in. Hg):
(•in): 720.00 Tunnel area (»2.ft2):
Chrg ut Hood moist (?. uet):
(Ib net): 25.00 Burn
run
time
(min)
0
60
120
180
240
300
360
420
180
540
£00
660
720
vel dp
(•« K20)
(in.H20)
0.058
0.059
0.060
0.062
0.057
0.058
0.061
0.060
0.060
0.061
0.060
0.059
0.058
tunnel
temp
(C.F)
80
78
80
72
109
92
84
80
83
83
80
93
90
DGH
rdg
(«3,ft3)
626.916
656.300
685.600
715.200
744.600
774.800
804.700
834.400
864. 100
893. 700
923.400
953.800
982.382
DGM
temp
(C.F)
69
78
85
82
88
92
91
91
88
87
84
86
89
Sanp vol
2 (s«3,scf)
1.046 260.897
0.99
28.56 Flou rate
21.64 (dsm3m,dscfn)
0.1963 153.47
10.02
rate (dry kg/hr): 0.85
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
550
550
vel
(•/•in)
(ft/«in)
1143.15
1150.83
1162.70
1173.13
1163.29
1155.79
1176.68
1162.70
1165.92
1175.60
1162.70
1166.76
1153.69
PR
(JO
102.
100.
97.
103.
102.
100.
97.
98.
98.
97.
104.
96.
6
3
5
3
7
1
1
8
7
9
3
9
dDGM
vol std
U3.ft3)
22.220
21.786
21.727
21.699
22.046
21.669
21.563
21.563
21.608
21.720
22.355
20.941
85.49
17.640
460.00
1850.00
vs/VnTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C.F)
0.01 1162.53 84.92 85.38
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample vbluii* Calculations
t-e
I
o
Stv canu:
Model no:
Lab name:
1st date:
Run no :
1st ti«e
(•in):
Chrg ut
(Ib uet):
run
time
Coin)
0
60
120
180
240
300
360
420
480
540
600
660
720
HflUGH'S PRODUCTS Units Unetric,
S173E 2=Eng!ish:
ES/CB Y, OGI1:
11-14-89 Pi tot co:
C-l-6 Gas NU :
Pb (an, in. Hg):
720.00 Tunnel area («2,ft2):
Hood noist (7. uet):
23.60 Burn
vel dp
(am H20)
(in.H20)
0.055
0.053
0.054
0.057
0.057
0.055
0.057
0.056
0.055
0.055
0.054
0.054
0.055
tunnel
temp
(C,F)
67
%
no
85
85
78
75
90
89
84
86
90
81
DGM
rdg
(<»3
985
1014
1043
1073
1102
1132
1162
1192
1221
1251
1281
1311
1341
,ft3)
.020
.300
.500
.000
.600
.200
.000
.000
.800
.800
.900
.700
.772
DGM
teirip
(C,F)
65
77
86
87
91
85
85
87
91
91
89
90
88
Samp vol
2 (so.3, scf)
1.046 260.394
0.99
28.56 Flou rate
21.53 (ds(i3m,dscf«)
0.1963 147.31
11.87
rate (dry kg/hr): 0.79
DGM dH
(am H20)
(in.H20)
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
vel
(n/ain)
(ft/«in)
1102.52
1111.67
1136.15
1141.40
1141.40
1113.97
1130.88
1136.52
1125.30
1120.16
1111.97
1116.04
1117.07
PR
(JO
106.
105.
97.
97.
95.
99.
101.
99.
99.
100.
101.
100.
2
3
8
5
6
1
1
3
4
5
4
1
dOGtl
vol std
(«3,ft3)
22.197
21.642
21.504
21.537
21.381
21.763
21.909
21.683
21.670
21.742
21.604
21.762
85.49
17.640
460.00
1850.00
vs/V«Ts vs ave tunnel DGM
ave temp ave teop
(C.F) (C.F)
0.01 1123.46 85.85 85.54
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED \\- C\ - S °]
DATE RETRIEVED P ^
WOOD SPECIES
WOOD MOISTURE (7. DRY) /2.,7'_-
• WOOD MOISTURE (I WET)
TANK 1 /* '7 5 (—IN HG) TEg. /"? (C)
TORR ABSOLUTE ~L.
POSTTEST B.P. 1 / . (,"% (IN HG)
TANK / "Z. / c 5" ("IN HG) TEMP. "2.2- (C)
WOOD CONSUMED (L3) /££ .'i (KG),
SAMPLE FLOW RATE PRETEST
ROTBHETER "7 V -(ML MIN) S' •
TORR ABSOLUTE
POSTTEST
ROTAMETER
•(ML MIN)
PRETEST LEAK CHECK
START 7.. '£- (IN H30) FINAL 7.^7 (IN H20) LEAK RATE O .• ~2- (IN K20 MIN)
POSTTEST LEAK CHECK
^ (IN H20) FINAL?, o (IN H2) LEAK RATE Q ,r> (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
C02(Z)_
CO(Z)_
02 (Z)
GKAMS MASS HrTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TINE
PRETEST t +52. MIN- •*• MIN. * MIN. + MIN. DELTA
SAMPLE LIME
CONNECTOR
LOT,
J-C-1-7
-------
t-,
I
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I
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PARTICULATE WEIGHTS SUMMARY
Page.
of /
CLIENT L^ I'/t RUN No. 1//V - C I Placed in Dessicator: Date/Time //- / V 8 7 C^V)/3 ^
ES PROJECT £ P I Z "$ STOVE MODEL No. S~ / 7 3 ^
POSTEST
1
• WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
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RELATIVE
HUMIDITY
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I
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-------
I
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I
PARTICIPATE HEIGHTS SUMMARY
Page.
of.
,CLIENT .
ES PROJECT
RUN No
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• <• Q)
"
STOVE MODEL No. S'~
POSTEST
Acetone Lot II 9 // ^
Acetone Sample Volume *?
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
• .
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WT 2 .
WT 3
WT 4 •
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NET
DATE /TIME
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tf ' 7h
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77. 7^yy
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WT AMOUNT =
PRE WT
^^^ t'T.&tl
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ROOM CONDITIONS
RELATIVE
HUMIDITY
1 / <&7
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BAROMTRC
PRESSURE
'Z-//?
?/.~7
Initials
/^X?
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(C)
TOTAL PARTICULATE CATCH (A-i-B-i-C) =.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
I
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,CLIENT _
ES PROJECT Afi /1~*> STOVE MODEL No.
POSTEST
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Acetone Sample Volume
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
••
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NT 4 •
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NET '
DATE /TIM IS
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ll-itt^rt/o
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PRESSURE
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/^^X?
/^'c^
(C)
TOTAL PARTICULATE CATCH (A+B'C) =.
-------
I
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I
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY ^ Patje___/ of '_
RUN No. c><":" •( /-/ Placed in Dessicator: Date/Time //•- ct ~\
- /~>. ?.
STOVE MODEL No.
POSTEST
••
• WT 1
WT 2
WT 3
WT 4
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DATE /TIME
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(A)
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-------
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ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Pane L of /_
RUN No. 56--C- /-£ Placed in Dessicator: Dal
STOVE I10DEL No. __5 '
POSTEST
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
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WT AMOUNT =
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.$<»*
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(A) (U)
> •
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^ooc,
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ROOM CONDITIONS
RELATIVE
HUMIDITY
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PRESSURE
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-------
PARTICULATE WEIGHTS SUMMARY
Paye.
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STOVE MODEL Ho.5-/?^
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>
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WT GAINED
DATE /TIME
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FRONT
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/1/T-S/
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. 97
CALI13RATION WT.
WT AMOUNT =
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• fooo
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HUMIDITY
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Initials
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-------
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ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page / o£ _ Z _
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RUN Ho. - -•
STOVE MODEL Mo. .5
POSTEST
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WT 2
WT 3
WT 4
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WT GAINED
DATE /TIME
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WT AMOUNT -
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-------
t-l
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\J\
CLIENT .
ES PROJECT
/? "?
PARTICULATE WEIGHTS SUMMARY Page / of
RUN No. C ~/" ^ Placed in Dessicator: Date/Time.
STOVE MODEL No. , 5 ~ /7 ^^
POSTEST
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• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
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RELATIVE
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Initials
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(A)
(B)
-------
CLIENT £/V?
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page
RUN No. C" /" ^ Placed in Desstcator: Dal
STOVE MODEL Ho. $ - H3 £
POSTEST
/ of
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
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WT AMOUNT -
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t, 5 crt^c/
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PRESSURE
'Z./.Sf
2/*'7
Initials
/V^
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(A)
(U)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f 'P.-'/ -
ES Project I
'Wood Heater Model lVoc,W'~) S113'
/
Operators kj i\ l4 | A fl r^
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) lt&6(j Thermostat Setting
Primary Air Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest | Post Test
Zt.g \ T./.V •
/C, 4//C.C
O.cco
^«;
6
c
/0-c//;.o
. •
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
to
Actual Fuel Charge Wt. "!M,Cp
Fuel H20% Dry \U\\ Wet
Fuel: Dry Kg \1, 6^
By-pass
Door
Veloci ty Traverse
p Temp
A 1 SASfa _H
J?
2 0,C(f(
2 fl.QL7 J£L
4 S.CuS 51
LOADING/TEST START OPERATIONS
Air Settings
Comment s
6 1
Ave.
2 Aei^y
58
5S
^5_
Pitot Leak Check
Static
J-C-1-17
-------
— »
s^s
»^3)
TEHPEKATUUE AIIU FUEL CONSUMPTION
ENGINEERING-SCIENCE, INC.
CHunt &\1\ Run Jf C.-I"' Test Fuel
Date Ij-^B0!
ES Project 1
C-,
1 £C
0
1
i — >
I
i— »
CO
Time
Sampling/
Clock
(3050
01 5-7
1
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l^n^l
1 7 <7o
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-^.1=,^
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Fuel
Ht.
(Ibs)
~L.'-l
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7.v7__
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Uood Heater Model S|7^>.=- Coal Dcd
3> Operators \\V\\U i >\lxlv\
^Cii^- ?)"W-H"
Comments
. 1.«-C**-
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Left
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Temp .
5' "7
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96
96
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1
Room.
Temp.
S" ~\
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5~<7
•
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date f
-I-K i
Sampling Location
Sample Type
Run Number^
Operator
Ambient Temperature_
Barometric Pressure
Static Pressure, (P;
Filter Number(s)
Meter /
SAMPLING OATA
c.
Start Time
Stop Time
Probe Length and lype
Pi tot Tube Coefficient_
Assumed Moisture ~
Sample Box NumbeF" -ft
Meter Box
Meter H
,*/'/
Pretest Leak Rate . OOfj
Post Test Leak Rate .OP*-/
Gi. /0"
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock}
&
0 075o
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no
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TEMPERATURES
Di 1 u t>
-------
KfZS33 £73^1
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/
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-------
c
FUEL MEASUREMENTS
Date [\-°l~& I Wood Heater Manufacturer
Project No. fc ^ )"L.*S, Wood" Heater Model
Run No. r, — ( - \
Circle One: Pretest Fuel ^test~Fuel^. tipl^
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; Actual Load Weight
Fuel Piece Length .
Moisture Meter Calibration tar -2fflS- 11, • o
Moisture Content-(Meter - Dry Basis)—1
Piece No. Readings Average
2 /-.c //.£ /G.y
3 t/'l ll.lc //.J
4 (f^1* >/^ 2Z."7 26./
5
6
7 '7^-
8 h,'l- //."7 //. 2.
9
10
11
12
13
14
15
16
17
18
19
20
Overall .Fuel Moisture Average
J-C-1-21
-------
Client __
Date 11 ~\ 0-61
WOOD HEATER CERTIFICATION TEST INFORMATION
" II Run i C.-
ES Project f
j ^ V
"Wood Heater Model 5 H "S 6.
Operators ^^ . .\HX
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%}
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
TJ.<2£
0V
n
0
iCi.o / i^.c
tvLV.
Post Test
•^/,SC .
<&
^
/•i'C//C' O
•
•
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20% Dry
Fuel: Dry Kg
LOADING/TEST START OPERATIONS
By-pass
Door
Veloci ty Traverse
Air Settings
Comments
p Temp
A 1
2
3
4
B 1
2
3
4
Ave.
P
Pi tot Leak Check
Static
to
Wet
J-C-1-22
-------
C-l-7-
WOOD IIEATEIt CERTIFICATION TEST
TEHPEUATUIIE AMU I:UEL COMSUMPT10K DATA SHEET
ENGINEERING-SCIENCE, INC.
Client /?/>/; Run I C
Test Fuel Charge
. Page / of )
Date )l ~ /o>- 'Acl Vlood Heater Model S-/7"V: Coal Ocd
ES Project t
<-,
I
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to
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"line
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Clqck
£}"7&o
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(760
/ *^r)
/3aV
'2.00(5
<2,|(iC>
Test
:uel
Ibs)
I.C>
5". 2.
2 j ?>_
f^L.i./
C: .11
~\,o
"Z-. "2-
/t' , 1
-7.0
^£2
/^j, ~2_
6. T—
*, /I
T5>,l>/'S
>i?Hl
*Ci37
,011.
^,0^/6
o,CY3
/("SS
,/i-i«j
fC''2.~2-
iO/T
.01 ^
-
AP /2 ^ Operators /?^/J ^9 //
Comments
^.H/Hj '1.R-&- ocWc7e(
-------
ENGINEERING-SCIENCE, INC.
Hood Heater 5
C-l
o
SAMPLING DATA
Date //- /(, - $••/
Sampling Locition_
Sample Type
Run Number_
Operator
Start Time
Stop Time
- /- "Z.
Ambient Temperature
Barometric Pressure
Static Pressure, (P.J
Filter Number(s)
Meter /,c>V£
//
Probe Length and Type
Pi tot Tube Coefficient
Assumed Moisture V^
Sample Uox Number C.
Muter Box Number £TP/l
Meter H
Pretest Leak Rate
Post Test Leak Rate
Read and Record All Data Every
Minutes
Clock Time
Sampling (21-hr
tlme.mln Clock)
O tf90<5
l*$
TO
y-i
&Q / 1 C» &
75
/6^
llO Vl0''-'
CSS
I'yO
io'j
(£>£, |7_co
11*)
2./D
Zt-1^
/,vo I "3 k*--*
c*5S
2_lO
16 'j
-^iC-
-*-yo
~~^L^ *—J
,-^ f. r> 1 S
Vel ocl ty
Head
( PS), in.
H20
0,0 56-
/ ) r\ ?> "/
O-OS^,
0.05^;
j. /< 5 /
* . ^ 2~
. bv 0 ^fS
A u rl £ ^)
RCcii
& C>LI
i O r>1
^ O^ "?
« CJ ? "S
•7 O^""^
Ti- o *7 Z,
> 0>5~~)
.o'J G
fi5 C>
ci^ <<-
05 1,-
. £357(1-
Ori fice
Djffere
( H), in
Desi red
. ^^
ressure
ntial
H20
Actual
,S'S
.S'S
• t>-S
t^c,
.S'S
<,^^
. A ^
* *>^
> r> 5"
,53
^ C^
^ ^ "S
» f7^"
, <5 ^
^ 6 *n
- 'JS'
, ->^
u 5 "f
• SS
. y s
. -5S
, <; X
TEMPERATURES
Di lution
Tunnel
|
Meter
In
£>6'
"7~1
'*?/
C1^>
^o
lo
7
Meter
Out
6>ci
S"^
q 9
qc:/
9T
"•y f>
'? "Z-
Filter
•
Impinger
66 .Vv •
-77 JTz^
"S'^i ^*7
7<^ <^Z.
2>/ • 57
&i s"§
A-o s— 7
Pump
Vacuum
1n. Hg
1
\
/
/
/
1
/
Flue Draft
1n. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood lleater_
Date
Sampling Location c-
Sample Type KS tr-
Run Number CL—/ - 7
Operator
• ^x. Clock Time
Sampl 1 ngxJZI-hr
time, m1n^vf,lock)
. * "~ .
•3HS
<-/ / ~1& &
Y7.S
S.t a
525
5YO /?OC3
5^e;
570
58*5
£,OO f £)£>O
61-3
fcl£>
fai
<=? 7 C, 6
ttSj'?
6^5>o
Veloci ty
Head
6,05s
i OS "2—
1 ^S*- ^
NoS j
. O*7 Y
*o'?~-i,
A "
Actual
^5S
.SS'
L RS
^^^
. 53
,5>S
« ^^i
> IS'
.55"
, 5-^-
*• SS
' 5<"
,<5 s
t^^
1 "^ *i"
•"^"S
^>t>
( 55
. 5"?
-S^'
, 5^
TEMPERATURES
Dilution
Tunnel
j
Meter
In
£//
cfc
')/
9 o
9 7_
-
Meter
Out
ci/
S'z
^>o
Impinger
6? Z-
^S"
6'S7
5~C
•
."? ^
Pump
Vacuum
in. Hg
/
/ •
/
/
/
Flue Draft
in. H?0
I
o
-------
FUEL MEASUREMENTS
Date n 1* < _ Wood Heater Manufacturer
_ _
Project No. _ ___ Hood" Heater Model -g, ;-] "S
Run No. _ _
Circle One: Pretest Fuel (Test_Fue
Fuel Type and Amount 2x4 _ 4x4 1x4
Ideal Load Weight _ ; _ Actual Load Weight
Fuel Piece Length _ . _
Moisture Meter Calibration— 125 _ — S3X— . "2-3
Vjovd Tt^-S. °F _
Piece No.
2
3
4
5
6
7
8
9
10 ^
12
13
14
15
IS
17
18
19
20
Moisture Content-(Meter - Dry Basis}- CorvccTc.ci
Readings Average
7,1 ILL, /O. -7
/o.3 //.? /2.r
?./ /a.? °< i
//,G //y // o
/C,f //, Z /c, 9
__L, __
Overall .Fuel Moisture Average
J-C-1-26
i PW'
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client £/>/} Run t d" - /- "?
Date ~
// - 3
ES Project I %D
Wood Heater Model
Operators
/ 7 3 ~
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
-2, AC?/
7^
/**
n
k>.f/&.e>
Post Test I
2/.7S • 1
*•«
/V
£)
to.* /to*®
\
/Vd
•
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel HjCK Dry
Fuel: Dry Kg
to
l~l~J
ll,60(t?
LOADING/TEST START OPERATIONS
Air Settings
Comments
Ave.
Pitot Leak Check
Static
J-C-1-27
-------
ENGINEERING-SCIENCE, INC.
CHunt t>PA~ Run II
Date
HOOD IIEATEH CEKTinCATlON TIIST
TEMPEHATUUE AIIU FUEL CONSUMPTION UATA SHEET
Test Pucl Charge
Coal Bed
ES Project. I
Wood Heater Model ,*5 (
Operators
Page
I
o
I
K-
I
N>
OO
line
ampling/
lock
/o/o
/I IP
v ^
K/G
-1,1 10
est
uel
•/t.
Ibs)
:l,ue
Draft
2u±
3,2-
•7.
1.0
kfi_
6.ZG
AI
£
6V7
Comments
.«//.<»
1326
^,. 7
Couibustor Temp.
7.77
/ocr?
Surface Temp.
lop Rear bottom Right Left
232.
Stack
Temp.
2£L
I2Z
5V 6>
25^
on.
Tun.
Temp .
j£A
j£2_
^
Room.
Temp.
2<£.
J^L
-------
ENGINEERING-SCIENCE, INC.
Heate r fin
SAMPLING DATA
C-/-3
-/- •*
Wood
Date
Sampling Location
Sample Type
Run Number^
Ope rato r ,
Ambient Temperature
Barometric Pressure
Static Pressure,
Filter Number(s)
Meter £Pa
Start Time
Stop Time
/0/D
77?
Probe Length and type ,/fy
Pi tot Tube Coefficient *_$
Assumed Moisture V
Sample Box Number_
Meter Box
Meter H
Pretest Leak Rate _*GOl
Number
JVA
Post Test Leak Rate.oot. ^o
Read and Record All Data Every 6Q Minutes
Clock Time
Sampling (24-hr
tlme.mln Clock)
n loi&
10
V>
(.-£> \\\^
-75
1&
105
no |?..|0
/">'O
.(jC,
In
/£/$
210
ZiS
io I5i&
MS
-JO
•vi^^
O; /\ ( / 1 A
A(/'L' J 1 ** 1 *~*
Gas Meter
Reading.
(vm) ft3
H^/C-o
Cp'j,"-/
o'-J* ^
/<3 SV V
fofaty. o
(f\^.^
Velocity
Head
( PS), in.
H?0
(Ko'j'-y
nO'j^f
•Jt.1^0
v<>ci t
.05^/
, 05 ^
• o r> ."<»
, o 5 •— /
.O'viS
j. 0 c) '3
., ^55
i 65.'i'
1 0 *7£>
<0<73
J^> "5 "^
• c^^r "•?
*" C"?
„ CJ^~1
* Ct^, i '
f ^^1_
a C\ C\ ~L
r*^, 7
. 05^
Ori fice
Diffen
( H), in
Desired
-35
'ressure
>nt1al
H?0
Actual
-sS
_, 5"<5"
' *)*>
• 5£
. 5 S'
, S S"
'^^
• ?>r7~>
ff^C-i
' S S
,sc;
• £>£>
* *5 ^
•» 5"^
- ?^T
,. <^^
"^^~
4 CJ <\
. <^<>
<- ^^
» ^"^
•/^"T
, -j-'- $"^/
Py 5^>
& 3 5"6
Pump
Vacuum
1 n . Hg
/
/
^
1
/
/
/
Flue Draft
1n. H20
t-l
I
o
-------
SAMPLING DATA (cont.
I
o
I
OJ
o
ENGINEERING-SCIENCE, INC.
Hood Heater *?- / 7 J £~
Date
lh//^>;l
Sampling Locati
Sample Type 5<
on C /',-<; i//
\. Clock Time
Samp11ng\(24-hr
time, min\Clock)
\f," • -—JJaic^
•v?< • il-if^
~Tf\D '/I V<>
V" ^ /t *5 £
1/7 e n/o
•yso' ovt>
V6*i /T)/£> /«;•/<•;
^Z-S /Sfi
6/T -»,.";
^-^J lc'/Y.
/1»V5 7t-fiS"
"p= -Z//0
27*1 '2. '? *V
^tjO --2 cVi)
TO'5"<^-
^ <•) *j 'L.
..o 5 3
* ^^ .?
« ^ 5^'L
i. c- 5 t-
; ^>.'>7'
. O'iS
-OSS
• oss
,^S 3
/ o 5 V
. <^5*y
.^sy
-5 '• ^X'
«- ^ ^
f. •=, <^
, *7 ^
r 5"5
.66
" 55~
• 5"V
• 5"5
, s S
. s5
5 -5
,55
-•5S
55
. ^S
TEMPERATURES
Di lution
Tunnel
Meter
In
-33—
^-7
9?
73
r/5
Meter
Out
*? "^
9"Z
3 ?
ff~j
c^J^S
Hlter
76
b 7
79
ty/
7?
Impinger
6v
*r -s*
S~7
55" y
-
^<5*
Pump
Vacuum
in. Hg
/
y
/
/
/
Flue Draft
in. H?0
.55
-------
C-t-3
FUEL MEASUREMENTS
Date {{-{(-Q0! _ Wood Heater Manufacturer
Project Ho. |^ ,-;/>, Wood" Heater Model ~A-k
Run No. --- '
Circle One: Pretest Fuel C[est_Euel
Fuel Type and Amount 2x4 _ 4x4 Ix4_
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length _ . _
_
Moisture Meter Calibration W5^ _ _2»-
\j0*cl r< ~, o. °F _ • :
Moisture Content-(Meter - Dry Basis)—1
Piece No. Readings Average
1 £7C 15.7 /V.5 11.6
2 /5 //V //^
6 /few ^-7_^/f •
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Overall .Fuel Moisture Average ( J <.
J-C-1-31
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client (Ez^
Date
Run t
C-l'-
- £el
ES Project t
"Wood Heater Model
Operators \,v
\1
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr) , Q 5/ Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
-M,T2
(' —
,"-/
<0
£.u/f'i>iv.
Post Test
Z/.<*<; •
-?£.•
/6
C:
/o.o /,• ;• c;>
,\,' 'V |
TEST FUEL DATA
to
Actual Fuel Charge Wt. "2-5v
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2K Dry
Fuel: Dry Kg
to
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
p Temp
A 1
2
3
4
6 1
2
3
Ave.
Pitot Leak Check
Static
J-C-1-32
-------
WOOD IIEATEU CEKTiriCATION TEST
n
i
1
. 4
TEHPEKATUUE AND FUEL COMSUMPTIOH
ENGINEERING-SCIENCE, INC.
Client rVA Run f <— 'I-L( Test Fuel
Date
\V-VT- ^1 Wood Heater Model ^S \TSl~ Coal fled
ES Project f
Time
Sampling/
Clock
/too
JIAC3
i"2Ac>
/ -p,
fOcrf L.
3^
r ' ^
/y f -\
T'V
*^ 6.--
/i6>
Fl,ue
Draft
in
>i6zi(
C '.'VrC
o'37
u'VS
o3a
rOl*)
i>i)'/i>
a/rfo
.023
o/W
*{>•/£)
i^E-7
lQ?s~f
•
T\,uV2.]A Operators \/V)^V-\ L ol\i i\
Comments
<."M 'KK - -.S('\ 'r.«rx«-A
«-/.o/c,i/ ?'•.,(.-.'* vi.-i.-w- (. (o< . S
cuj- v^\c->c. >,-/ 7r //v'.i/ /;-z ?
fl.fj/l. 7_ ^.6ttl-. ,-f^./!-/ v-; M-V
J7.iy|- H'v- f,.J0{.'-.(' ^,. v"\i'V\.
l^pr-fU^f ^ 2fX/lf>,-ci r '•!,/''
1 7 /'I A)//1 ''/Vc/.'.c,- V /"«-• ;l, /I ',
21-
"?9 "S^
'"'I'V "^
120
" ?*V "7
DATA SHEET
Charge <-''_> i ^J>
Surface Temp.
lop
Hear
bottom
( 't^
n.z e
-7<-/5'
'z.'V'V
'Z.'y y
/99
^. vz.
"Z- V S'
'2- 3 c>
•2.O&
/ 9 9
?^ c 7
"^-/ "^
Kight
Left
Page / of
Stack
Temp .
"o2.?
ff
l^r
•^•^o
2^
f/ rt Cy
"^y^/
2
7?
7T
~7
& n
<&&
7 C
-------
ENGINEERING-SCIENCE, !NC.
Wood Heater ^> \~T\ E
Date \ I-17, -«£--,
SAMPLING DATA
c -/-
Sampling Location
Sample Type
Run Number
Ope rato r
Start Time
Stop Time
/fcc
Ambient Temperature_
Oarometric Pressure"
Static Pressure, (P;
Filter Number(s)
Meter J.owt
Probe Length and Type
Pi tot Tube Coeff1c1ent_
Assumed Moisture_
Sample Uox Number_
Meter Box Number
Meter
H
»\.\C
Pretest Leak Rate
Post Test Leak Rate
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
D /ooo
it
^^
V-v
t,c. /I00
7S
"-/c
/••>6
,2o 1 LOO
/M
1 >"(•
/o r^oo
^5
c'O
? ? f
,) ^<3 /'/L^1
-, ^«-
"7C
l?-^
•"•^ I ')"^o>
-V-?
_ ..
•\- ,---,
,--\^i- ic,cc*
Gas Meter
*J ^ *u. , '5
Veloci ty
Head
( Ps).1n.
H20
,Oc;c-,
, OS'">
oSS
jC.'-^S
' ^ ^) ^
. 6 ^JS
, Cj ^ ^~/
. <3^"fJ
, c-s S*
.0 « 5~y
. , c ""^ *S
i O^)(f>
. 0 Ti C-
! OviS
i (.j ^ iz
* a S C
* f> 'T6
• 6&
r f) *>/,
^ f-i^^i
.. fj^.^
.<->$-?
Orifice
Djfferc
( H), in
Desi red
,*>•>
ressure
ntlal
H^O
Actual
-s *v
. ''S
> ^
.i-,^
'-,'S
')^
i t>"S"
. s ^
/s'^L
, r~iS
f ^^
r <7 f
0 "7 C
••*>*•>
r^^>
^ ^ ^
• $ "T
^ •5"^"
' T<~
•<•">
TEMPERATURES
01 lution
Tunnel
Meter
In
-70
5~i V1**
77
'J.S
9y
9cv
^i! S"i?
7^ • $^7
->/ S
-------
SAMPLING DATA (cont.)
C-/-V
ENGINEERING-SCIENCE, INC.
Vlood Heater
Date //-
Sampling Location_
Sample Type
Run Mumb e r C. - /' ~
Operator m c a
• \^ Clock Time
Sampl1ng\(24-hr
time, min^xClock)
~3£>7> £&££
i-}$ • /^
Wo 'to
i/o<; v
V?T 1C
y$ef ^fi
LJ6S V5
V^O / ^/y>
V9T /^
5*/^ 3^
<-?< V<
9-y« y 9c/<3
f ^"^ /9
C7rt '^
c^^7 y^
lp
-------
FUEL MEASUREMENTS
Date II - 17. ^'o Wood Heater Manufacturer
Project No. £ ^ ( 7, ^S Wood" Heater Model 'SiT^.^j u
Run No. r- \ — <—<
Circle One: Pretest Fuel Test Fuel
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; Actual Load Weight
Fuel Piece Length
Moisture Meter Calibration O3S- -225-
Moisture Content-(Meter - Dry Basis)- CoivscTti
Piece No. Readings Average
1 66 / z.o \IA
2
3
1 /2,7 /2.V //.?
8 /o>7 y^ /Ay
10 //./ //.£ >a,
11
12
13
14
15
16
17 __
18 •
19 __
20
Overall Fuel Moisture Average
J-C-1-36
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' • •' Run f C_~ /
ES Project f
"Wood Heater Model S / ~1 "b (=-
Operators U' M- 14. , ^ M CR
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (J)
Room Velocity (ft/oiin)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
Z i . -'^ ~i
6-1 9
/-?_
/
/ X
^ rx
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
to
Actual Fuel Charge Wt. Z5 0
Fuel H2OT Dry l7,|3 Wet /G.CZ.
Fuel: Dry Kg /C' '
By-pass
Door
Veloci ty Traverse
LOADING/TEST START.OPERATIONS
Air Settings
Comments
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pi tot Leak Check
Static
J-C-1-37
-------
WOOD IIEATEH CERTIFICATION TEST
TEMPEUATUIIE AMU FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
CUunt ;,9/VRun I
C-I-S
Test Fuel Charge
"2-5,0
Page ( of
Date \{- 1
ES Project 1
t-i
o
i
H-
1
to
CO
"line
Sampling/
Clock
cfeco
OC](.^J
j&eo
[f 00
/7,-o
I "\GO
/^O
i f*>O
l/fcrtG
ha d
t*
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number
Operator
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Start Time
Stop Time
Probe Length and Type /£•/•''
Pitot Tube Coefficient ..•? i
Assumed Moisture -V
Sample Box Number C,
Mater Box Number RAc <:s
Meter H J\} /\
Pretest Leak Rate .00 | e
±L /o
Post Test Leak Rate xoo / (^ ~V
Read and Record All Data Every („ 6 Minutes
Clock Time
Sampling (21-hr
time.mln Clock)
O O^oL?
; 'T
"XJ
•vv
60
Cc( C O
7*7
^JL>
IC'f)
!?(} /tX'o
/3S
Kr-
frr1!
(&C
lIC"^
fi^
T./^
?''S
? */o /z. -C~o
Z^ri
•i-'d"
2. f*li
"^'.t-' | "^C"-<^
" L^
,
"] | s , 2-
7 W. (^
—l--)i,/.£\
KnL/."7
Velocity
Head
HpV
)RC Y-J
. Cc-
, 6e7^-.
,, <^<\
- n < cl
iCiC, f>
. (•• >..- C •
. C& 0
, (3t>- C
,i3G ^_
.. OG Z
CC ' C
* *1 ^
, < JJ-
.'•'S
. r; r;
, •'-> s
, ^'C^ .
• "*'->
"S S
s"-^
ss
> -.•> -i
. <7^7
4 T^
. />' S
' ^"S"
, ^^
' •> S
r
TEMPERATURES
Dilution
Tunnel
1
Meter
In
(Sv
o £
.^
7?
7/
Filter
7,^>
Impinger
'
7
VO
-------
SAMPLING DATA (cont.)
Hood lleaLer
I
o
I
I—'
I
*-
o
ENGINEERING-SCIENCE, INC.
Date //-/^-S"1) 7
Sampl 1
Sample
' ^
ng Location C'/iff Fee/ £~V\Te
Type 5"6
Run Number (""* - / - S>
Operator /&?* A *<>//
\. Clock Time
Sampl 1 ng\(24-hr
time, min^^Clock)
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TEMPERATURES
Ji lution
Tunnel
1
'leter
In
y'v-:
C/C/
9 -S
^io
Cf /
-
Muter
Out
V /
^1
¥ ¥
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77
77
7~7
7 Z-
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Impinger
.sJ.-
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s"'/
SS
•
5 o
'urnp
Vacuum
in. Hg
/
/
/
/
/
Flue Draft
in. H?0
72.0
-------
C-l-5
FUEL MEASUREMENTS
Date \\-\3"^n Hood Heater Manufacturer
Project No. £.>> \~J ^ Hood" Heater Model s (~ T. c=.
Run No. C - \ -C-, ~~~^~~
Circle One: Pretest Fuel • Test Fuel
Fuel Type and Amount 2x4_ 4x4 1x4
Ideal Load Weight ; .Actual Load Weight
Fuel Piece Length .
Moisture Meter Calibration W5 -ess 3 "^ , /
Moisture Content-(Meter - Dry Basis}—1
Piece No. Readings Average
S \l±_ (l&_ jib
6 /31_ (^ (3,L
8 ( -' y.y
L> i ~^~
s //.?•
10 //. / //./ Ks-
11—. //./ ft./; ?.^
13 /^C. //.L //.*
14
15
16
17
18 -
19
20
Overall Fuel Moisture Average
J-C-1-41
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run / O^/'~
ES Project I
"Wood Heater Model [l^o ^ W \
i ! / . i
Operators US ^
^ K-. (\
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings __
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidi ty (I)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
2.1- 5^
£ z-
/ s
o
if. <^//L,O
AJA.
Post Test
Z./.S2. •
& y
i-f
&
tO,f//f>, 0
/
TEST FUEL DATA
to
Actual Fuel Charge Wt.
13-0
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20% Dry
Fuel: Dry Kg
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
6 1
2
3
4
Ave.
Pitot Leak Check
Static
to
J-C-1-42
-------
ENGINEERING-SCIENCE, INC.
CHunt £PA-
HOOD IIEATEU CERTIFICATION TEST
TEMPERATURE AMD I:UEL COHSUHPT10II UATA SHEET
Test Fuel Charge
Page
of
Date //-/6/~^> 7 Wood Heater Model Coal Oed
ES Project f
I
o
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Sampling/
Clock
6-700
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7V
(?£/
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAW LING DATA
it_^ V
-TT
Sampli ng Location
Sample Type
Run Number r _
Operator
//-<"-/-
Ambient Temperature ^
Barometric Pressure
Static Pressure, (P^T
Filter Number(s) ]
Meter
l.Q'-nv
Start Time
Stop Time
Probe Length and Type_
Pi tot Tube Coefficient_
Assumed Moisture L/
. ltcf
Sample Box Number ^*
Muter Box Number_
Meter H ~~
RI
Pretest Leak Rate
Post Test Leak Rate
Read and Record All Data Every Ml
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
0 C,1£>0
15
7<£>
Vs
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Gas Meter
Readi ng
(vm) ft3
"tr-^.o iO
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C,V 3 .S
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( H), 1n. H?0
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TEMPERATURES
Di lution
Tunnel
i
Meter
In
(,, c;
£-7
91-/
'IS
,9^J
<9 /
Y/
Meter
Out
4,^
71
^C-
-y?
?/
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,
Pump
Vacuum
in. Hg
/
/
/
/
/
/
/'
Flue Draft
in. H20
t-,
I
n
-------
SAMPLING DATA (conI.
Hood Healer 5 -
o
I
hNUINhtRING-SCIENCE, INC.
Date //. ;t/~ $ •-)
Sampling Location cT/< ? ^ VecS ^-2??
Sample Type ^<
^-
^ir ,
Run Number (~ -/- &>
Operator /£//••/? 'ct> //
"X. Clock Time
SampllngX^ZA-hr
time, min^vClock)
^£0 ' — L2i°o_
•37^" . /<•
3*fo 1/y
tfr><> yc
tyZtf IL/C'LJ
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Gas Meter
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TEMPERATURES
Dilution
Tunnel
Meter
In
•^v
^^?
9-7
*?/
c/'6
-
Muter
Out
§7
<.f /
9/
^9
Oo
Miter
T~'f
<*?/'
7 ^
7*r
Impinger
60
S"7
5?
$-<^
•
'•>"'ri)
Pump
Vacuum
in. Hg
/
/
/
/
/
Flue Draft
in. H90
-------
FUEL MEASUREMENTS
Date _ (j- U/^o ] _ Wood Heater Manufacturer
Project No. _ Hood" Heater Model
Run No. _
Circle One: Pretest Fuel Test Fuel
Fuel Type and Amount 2x4 _ 4x4 1x4
Ideal Load Weight _ ; _ Actual Load Weight_
Fuel Piece Length _
Moisture Meter Calibration 12i _ 225
vJwd T, ~, o. °F _
Moisture Content-(Meter - Dry Basis)- CorvKTtci
Piece No. Readings Average
i u-e° zt*_[_y7_7_ 2/7
2 tLH_ii^_ /_!_£= _____
3 f/'l ;/.? /^e
4 / ->» //.o ([//_ /7,0
5 //,7 fl.l _/£• <>
6 /7.y /io_ ALC/
7
8
9
10
11
12 ;?.Z /J,Z /2.7
13
14
15
16
17
18 ._ .
19
20
Overall Fuel Moisture Average l^'H, I
J-C-1-46
-------
TEST SERIES
C-2
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
i-o
I
Stv «anu: HflUGH'S PRODUCTS Units )-metric,
Model no: S173E 2=English:
Lab name: ES/CB y, D6M:
1st date: 11-15-89 Pitot co:
Run no : C-2-1 Gas Mil :
1st time Pb (mm, in. Hg):
(min): 600.00 Stack area (m2,ft2):
Chrg ut Mood inoist (.?. uet):
(Ib uet): 25.10 Burn
run
time
(min)
0
60
120
180
240
300
360
120
180
510
600
vel dp
(mm H20)
(in.H20)
0.055
0.053
0.050
0.052
0.051
0.051
0.051
0.051
0.051
0.052
0.050
tunnel
temp
(C,F)
63
%
1 05
93
8?
8?
85
80
83
86
9?
OGM
rdg
(m3,ft3)
351.610
383.800
113.100
112.800
172.100
501.600
530.800
560.600
590.100
620.000
619.952
DGM
temp
(C.F)
60
71
82
85
81
85
89
88
88
89
89
Saihp vol
2 (s»3,scf)
1.016 219.018
0.99
28.56 Flou rate
21.76 (ds*3m,dscfm)
0.1963 116.75
10.50
rate (dry kg/hr): 1.03
DGM dl
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
vel
(n/nin)
(ft/min)
1092.61
H05.91
1082.81
1092.16
1107.22
1 107.22
1105.19
1100.11
1103.16
1085.53
1075.12
PR
(?.)
106.1
105.5
103.2
101.3
98.8
98.3
98.8
100.0
99.6
101.3
85.19
17.610
160.00
1850.00
dOGM
vol
(•3,
22.
22.
21.
21.
21.
21.
21.
21.
21.
21.
std
ft3)
575
292
811
812
586
517
829
869
722
911
vs/VmTs vs ave tunnel OGH
ave temp ave teup
(C,F) (C.F)
0.01 10%. 12 80.17 83.00
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
O
NJ
Stv manu: HflUGH'S PRODUCTS Units l=metnc,
Model no: S173E ^English:
Lab name: ES/CB Y, OGM:
1st date: 11-16-89 Pitot co:
Run no : C-2-2 Gas MM :
1st time Pb (mm, in. Hg):
(mir>): 840.00 Tunnel area Cm2,ft2):
Chrg ut Hood moist (?. uet):
(Ib uet): 2?. 60 Burn
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
780
840
vel dp
(mm H20)
(in.H20)
0.050
0.048
0.050
0.051
0.050
0.050
0.052
0.050
0.051
0.051
0.051
0.053
0.051
0.051
0.052
tunnel
temp
(C,F)
74
93
87
94
92
81
85
93
89
84
85
84
82
81
80
DGM
rdg
(*3,
650.
680.
710.
740.
770.
800.
829.
859.
888.
918.
947.
977.
1006.
1035.
1065.
ft3)
952
100
300
300
100
700
600
100
600
300
700
200
400
700
035
DGH
tenip
(C,F)
66
82
88
93
84
84
84
87
92
91
88
90
88
89
87
Samp vol
2 (smS.scf)
1.046 304.293
0.99
28.56 Flou rate
21.68 (dsm3m,dscf,ii)
0.1963 141.81
10.83
rate (dry kg/hr): 0.80
OGM dH
(
-------
Method 56 Proportionality Rate, Flou Rat9,
Burn Rate, and Sample Volume Calculations
o
I
ro
I
U)
Stv manu: HflUGH'S PRODUCTS Units ^metric,
Model no: S173E 2=English:
Lab name: ES/CB Y, 0611:
Tst date: 11-17-89 Pitot co:
Run no : C-2-3 Gas MU :
Tst time Pb (mm, in. Hg):
(min): 840.00 Tunnel area (m2,ft2):
Chrg ot Hood moist (.?. uet):
(Ib uet): 42.40 Burn
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
660
720
780
840
vel dp
(mm H20)
(in.H20)
0.054
0.050
0.052
0.051
0.053
0.055
0.055
0.053
0.053
0.055
0.053
0.055
0.054
0.050
0.051
tunnel
temp
(C.F)
70
103
90
93
95
69
74
98
85
82
84
89
85
107
95
OGM
rdg
(«i3,ft3)
68.548
97.600
126.900
156.300
186.000
216.000
245.500
274.600
304.300
334. UOO
363.700
393.000
422.400
451.600
481.276
DGM
temp
(C,F)
67
82
89
89
91
82
67
78
86
87
86
86
87
87
86
Samp vol
2 (sm3,scf)
1.046 304.295
0.99
28.56 Flou rate
21.66 (dsm3m,dscfm)
0.1963 144.45
16.69
rate (dry kg/hr): 1.14
DGH dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
550
550
550
550
vel
(m/min)
(ft/«in)
1092.27
1083.26
1091.88
1084.28
1107.33
1101.29
1106.48
1110.32
1097.31
1114.74
1096.30
1121.92
1107.61
1087.10
1036.24
PR
(.?.
105
101
100
102
96
97
102
100
99
97
99
96
101
102
)
.0
.4
.2
.3
.1
.5
.9
.1
.3
.9
.3
.7
.0
.4
dDGM
vol std
(m3,ft3)
22.073
21.645
21.442
21.661
21.801
21.793
22.110
22. 104
21.780
21.740
21.487
21.560
21.374
21.723
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGH
ave temp ave temp
(C,F) (C.F)
0.01 1099.22 87.93 83.33
-------
Method 5G Proportionality Rate, FIou Rate,
Burn Rate, and Sample Voluine Calculations
o
I
N)
Stv manu: HOUGH'S PRODUCTS Units 1-metric, Samp vol
Model no: S173E 2-English: 2 (smS.scf)
Lab name: ES/CB Y, DGM: 1.046 260.648
1st date: H-18-89 Pilot co: 0.99
Run no : C-2-4 Gas Mil : 28.56 Flou rate
1st time Pb (mm, in. Hg): 21.82 (dsm3,B,dscfi»)
(ain): 720.00 Stack area (»2,ft2): 0.1963 140.73
Chrg ut Hood moist (.'/. uet): 14.41
(Ib uet): 34.80 Burn rate (dry kg/hr): 1.13
run
time
(ain)
0
60
120
180
240
300
360
420
480
540
600
660
720
vel dp tunnel
(mm H20) temp
(in.H20) (C,F)
0.050
0.050
0.052
0.050
0.050
0.050
0.050
0.051
0.047
0.050
0.050
0.050
0.050
72
89
88
86
83
85
95
87
109
93
86
96
94
DGM
rdg
U3,ft3)
484.
512.
541.
570.
600.
629.
659.
688.
718.
747.
776.
806.
835.
608
600
600
800
200
800
400
800
000
200
400
800
450
OGI1
temp
(C,F)
64
77
83
84
88
89
86
84
85
84
86
85
85
DGM dH
(cm H20)
(m.H20)
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
550
550
550
550
550
550
550
550
550
550
0.550
0.
0.
550
550
vel
(ft/ain)
1049.15
1065.78
1085.89
1062.86
1059.94
1061.89
1071.59
1074.42
1051.96
1069.65
1062.86
1072.55
1070.62
PR
100.7
100.0
97.4
99.5
100.1
101.5
99.0
102.4
101.5
98.7
104.9
97.8
85.49
17.640
460.00
1850.00
dDGM
vol std vs/VmTs vs ave tunnel DGM
(»3, ft3) ave temp ave temp
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.
22.
21.
(C,F) (C,F)
547 0.01 1066.09 89.46 83.08
783
691
799
787
747
719
651
611
651
458
204
-------
Method 56 Proportionality Kale, Flou Rate,
Burn Rate, and Sample Volume Calculations
c_
O
N>
I
Stv «anu: HflUGH'S PRODUCTS Units l^metric,
Model no: SI73E 2-English:
Lab name: ES/CB V, DGM:
1st date: 11-19-89 Pilot co:
Run no : C-2-5 Gas MU :
Tst time • Pb (mm, in. Hg):
(«in): 720.00 Stack area (»2,ft2):
Chrg ut Wood moist (?. uet):
(Ib uet): 27.40 Burn
run
time
(min)
0
60
120
180
210
300
360
420
480
540
600
660
720
vel dp
(mm H20)
(in.H20)
0.055
0.053
0.055
0.056
0.056
0.055
0.056
0.055
0.055
0.052
0.052
0.052
0.055
tunnel
temp
(C,F)
71
104
88
88
89
90
85
91
94
109
103
94
87
OGM
rdg
(m3,ft3)
837.003
866.000
894.300
924. 100
953.200
982.300
1011.600
1040.800
1070.000
1099.100
1128.300
1158.700
1187.348
DGM
temp
(C.F)
65
78
83
87
90
92
91
87
90
92
94
94
91
Samp vol
2 (smS.scf)
1.046 259.838
0.99
28.56 Floo rate
21.94 (dsmSm.dscfm)
0.1963 146.86
15.97
rate (dry kg/hr): 0.87
DGII dH
(mm
(in
0
0
0
0
0
0
0
0
0
0
0
0
H20)
.H20)
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
0.550
vel
(m/min)
(ft/*in)
1096.31
1109.13
1113.72
1123.80
1124.82
1115.75
,1120.72
1116.76
1119.80
1103.47
1097.64
1088.83
1112.70
PR
(7.)
107.
98.
101.
98.
97.
97.
93.
99.
101.
101.
104.
'93.
2
0
8
0
6
8
3
9
4
8
5
0
dOGH
vol std
U3,ft3)
22.401
21.334
22.258
21.576
21.458
21.528
21.493
21.650
21.458
21.454
22.255
20.973
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1111.04 91.77 87.23
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
CH
I
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I
Stv manu: HflUGH'S PROOUCTS Units ^metric,
Model no: flK-18 2-English:
Lab name: ES/CB V, DGH:
Tst date: 11-20-89 Pitot co:
Run no : C-2-6 Gas MM :
Tst tine Pb (mm, in. Hg):
(«in): 180.00 Tunnel area ((i,2,Ft2):
Chrg ut Hood moist (?. uet):
(Ib uet): 15.80 Burn
run
tine
(min)
0
60
120
180
240
300
360
420
180
vel dp
(oun H20)
(in. 1120)
0.050
0.050
0.050
0.051
0.051
0.051
0.052
0.051
0.053
tunnel
temp
(C.F)
72
90
9?
98
91
125
94
88
85
DGM
rdg
(m3,ft3)
189.90?
218.200
246.500
275.400
304.500
333.800
363.300
393. 100
422.943
DGM
temp
(C,F)
69
80
88
92
94
94
93
91
91
Samp vol
2 (sn.3,scf)
1.046 | 171.798
0.99
28.56 Flou rate
21.84 (ds«3m,dscfm)
0.1963 141.70
12.46
rate (dry kg/hr>: 0.78
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
vel
(m/min)
(ft/min)
1048.67
1066.26
1073.02
1084.67
1077.85
1110.60
1091.32
1074.91
1092.78
PR
CO
102.9
100.5
100.6
98.3
105.3
97.5
99.3
100.8
65.49
17.640
460.00
1850.00
dOGH
vol
(m3,
21.
21.
21.
21.
21.
21.
21.
21.
std
ft3)
593
158
291
283
352
498
756
866
vs/VmTs vs ave tunnel DGM
ave teinp ave temp
(C,F) (C,F)
0.01 1080.01 93.33 88.00
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED
DATE RETRIEVED
TEST LOCATION
SAMPLER SN!! MIN) 5 1
POSTTEST
ROTAMETER D -(ML MIN)
(IN H20) LEAK RATE -
(IN H20 MIN)
(IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(Z)_
CO(Z)
RUN COMMENTS:
• \\ ._
S- k P,1 '^ n
GRAMS MASS AFTER FLOW IMS 0.5 1pm NITROGEN FOR INDICATED TIME
PRETcST •<- MIN. + MIN. + MIN.
MIN.. DELTA
£/0^PROEE+FITTING
SAMPLE LINE
CONNECTOR
J-C-2-7
-------
t-l
I
o
I
N>
I
oo
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
HUN Ho. OPZ-C.-I' Placed in Dessicator: Date/Time /A
STOVE MODEL Ho. /V/?*-y i)f"$ -5V7?£
POSTEST
'
• WT 1
WT 2
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WT AMOUNT =
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.
-------
CLIENT £"'/'/?
PARTICIPATE WEIGHTS SUMMARY Page of
HUN No. I/PJ-C ^-Placed in Dessicutor: Date/Time//- 2 /-3*? ,
ES PROJECT f( O / 2- "\ STOVE MODEL Nc
POSTEST
Acetone Lot II *?// ^.
Acetone Sample Volume /->
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WT 3
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DATE /TIME
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WT AMOUNT
PRE WT
*/t/2
(C)
TOTAL PARTICULATE CATCH (A-i-B+C) =.
_mg.
-------
..CLIENT _L
ES PROJECT ftf) /Z'3 STOVE MODEL No.
POSTEST
PARTICULATE WEIGHTS SUMMARY Pat's of
HUH Ho. I - "£. Placed in Dessicator: Date/Time_ZA_
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Acetone Lot II N // O.
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HI, IV*}
'•>f . cc~ c^
POST WT
*:>*<., 066*
//v.
ROOM CONDITIONS
RELATIVE
HUMIDITY
; i %-5-.
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PRESSURE
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/^
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(C)
TOTAL PARTICIPATE CATCH (A-i-B+C) =.
-------
c_
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CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Pa^'e / o£
RUN No. C. - ?-/ Placed in Dessicator: Date/Time//-/<£ " '
,<£>
c/Q
/23
STOVE MODEL N o .
POSTEST
'
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
//-/6<4"/VA,
//-/$& mo
u-n& ins
.11-3 ~ 5 7o
< <£> 2> 7<5
-<,7?7
, *c>73
CALIBRATION WT.
WT AMOUNT =
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* ^oot,
.V11<\
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POST WT
9 ^ CT&tt
.flW
^^g
ROOM CONDITIONS
RELATIVE
HUMIDITY
•2V<9£-?
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PRESSURE
?-/.->
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,
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(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT .
ES PROJECT
EPA
RUN Ho. C.-2-~2- Placed in Dessicator: Date/Time/A/#- fr ?
J2 3 STOVE MODEL No.//4
POSTEST
•
• WT 1
WT 2
WT 3
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WT GAINED
DATE/TIME
//-/* <& 10 $0
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WT AMOUNT =
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, ^tC't-o
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V *,&<<&
• *rf
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to
»—«
NJ
(A)
(13)
-------
PARTI CD LATE WEIGHTS SUMMARY
£-1
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Patje
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CLIENT
ES PROJECT
£7 XZ
RUN Ho. C- ~i~ 2 Placed in Dessicator: Date/Time.
STOVE MODEL Me
POSTEST
// V 5
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• NT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
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/~\
//-/^/w
/'-3-39
FRONT
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CALIBRATION WT.
WT AMOUNT =
PRE WT
4 tjtrt'b
. HW*}
POST WT
* ^c'C'-t
. Srt'-L.
ROOH CONDITIONS
RELATIVE
HUMIDITY
/2^y
Tz^ I*
BAROMTRC
PRESSURE
2 /, -s
22^-
Initials
,
>*>'#
#*/%
(A)
(B)
-------
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUHHAUY Page _ of
RUN No. C~ -"Z-'Vplaced in Dessicalor: Date /Time. •'/'.
STOVE MODEL Ho.
POSTEST
_£'
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
//- !<$*} IH^O
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.6773
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CALIBRATION WT.
WT AMOUNT =
PRE WT
- *>&&&
t, ^ fts-O
POST WT
^^•2-
^ 5^* i*
ROOM CONDITIONS
RELATIVE
HUMIDITY
•^^7o
«fl? 7/7
BAROMTRC
PRESSURE
a2,<9
7 A 9
Initials
facA
/^/f1
n
(A)
(B)
-------
PAnTICULATE WEIGHTS SUMMARY
Pat'e
of
CLIENT
ES PROJECT A/)- IT- 3
RUN No. C- ^ ~:S Placed in DessicaLor: Date/Time //-/*? ~*
STOVE MODEL No.^^-^/if 5 J>-/?]?-/-
POSTEST
?. 2 ^ o
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WT 2
WT 3
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TARE WT
WT GAINED
DATE/TIME
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WT AMOUNT
PRE WT
,SWr>
x- /
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-
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^(r^,0
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ROOM CONDITIONS
RELATIVE
HUMIDITY
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PRESSURE
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Initials
,
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(A)
(B)
-------
CLIENT £rfi
ES PROJECT A D *
PARTICULATE WEIGHTS SUMMARY
RUN Mo. C* 'Z~ Q> Placed in Dess icator:
of.
Date/Tiinej2ll£L^l.
STOVE MODEL Ho.
POSTEST
It f ? 5 '
"•
• WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
11-11 (SJ&<(<;6
li- ~L / & /-i Vo
//-3-^')
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.6r6£
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client £fiA Run / C'- Z —
Date //. /
ES Project f ft. f) - I 2 '*
"Wood Heater Model
Operators
L,
/-/
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (I)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Ht.
Actual Fuel Charge Wt.
Pretest
•2. ?>->-)
6/
/c
C
/<•< (•//,< c
(
Post Test
-Z.l.~7~? •
-I/
/ —
c?
/O i- / i & - <--
/ / ///
TEST FUEL DATA
to
to
_£/_
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel K2« Dry !l "I.""' Met II.'
Fuel : Dry Kg •'. < .*\ i _-
LOADING/TEST START OPERATIONS
Air Settings
Comments
Ave.
Pitot Leak Check
Static
J-C-2-1
-------
ENGINEERING-SCIENCE, INC.
Client £ PA
HOOD IIEATEH CERTIFICATION TEST
TEMI'EHATUIIE AIIO FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page of
Date y/-A5 #7 Wood Heater Model <>• /73k- Coal Oed
ES Project 1 /} £) /Z3 Operators S)/<~/{ L() //
«-.
o
i
to
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'line
Sampling/
Clock
// "*>&
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-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
z-
Wood Heater
Date //
Sampling Location V"/i
Sample Type_
Run Number C - Z - /
Operator /it c
Ambient Temperature 6 O
Barometric Pressure 2 /> 7'7
Static Pressure, (Pj)
Filter Number(s)
Meter /,<
Read and Record All Data Every
Start Time
Stop Time
Probe Length and Type \
Pitot Tube Coefficient_
Assumed Moisture V •'%,
Sample Box Number_
M^ter Box Numbe rjl
Meter
99
Q-
II
Pretest Leak Rate d.Co^
Post Test Leak Rate
Minutes
Clock Time
Sampling (24-hr
tlme.min Clock)
| ) / 3/6
/*•> "?,c>
-^f> //5
VT /Vft>
L'r> /Y/5
"7 ^
76
/?o ;cv/'S'
(3S x
|<5O
l&^
1 fiO CO. ( ^
|f^C,
"cUC>
7 2"^
->^/o |~) I C
"i°7S
ZTO
2CL*L
-^ l> ^
'2^*^*^ 1 ^j i tr
•%iir J
— V.-VO
'"V-*"^
T.OO - f 1 I *=>
Gas Meter
Readl ng
(VJ ft3
5B5*. £>
HI '*>•'-/
H ^2 A f>
t^l2. V
"=^> 1 Cu
*r ?o, 5?"
Vel oci ty
Head
» f* ' '
0 & / (fi
. o <; -i
,o<:3 ^S
,05 2_
.(iS X,
. a r.' T 2
„ c7 5 "2-
» <^ 5 2.
.» o 97
, C> ^<-f
, tS CJ --/
, c')S t-/
,OS-\
, os^
, 0>cl ^
^•r^/
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1 05 v
_ <-> «; v
Orifice 'ressure
Di fferential
( H), in. H?0
Desired
Actual
c 5^
. 5 5"
c "5" 5"
,. C- 5"
/• fJ^
^rs
• S"S
iS" ^
. 55
. ^s"
. ft-<^
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„ 5-5"
, <7'5~
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7«V
Meter
Out
•
Impinger
•^^ •
7^ V ?>•
VS'
-------
=«a
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
Date //-/<
Sampliwj Location
Sample
Run Numb ere - Z -/
Operator /^ c /{ tL\
C - 2
• ^\^ Clock Time
Sampl1ng\(24-hr
time, min\Clock)
"\(?r\ — ' — • &{£.
^?7T • "?,-,
39o .-/v
VoC ^70
V201 T.CI/S-
y^? -VJ
V-5o- HS
V/>< t>z>
v?^ a//
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TEMPERATURES
Ji lution
Funnel
«^y
^^-
"tcter
In
1Y
yi
9^
^y
-
Meter
Out
95
e^
*9
#?
Kilter
7 5
76
% 0
•3?'
Impinger
*;9
•£0
^^
^s
•
3ump
Vacuum
in. Hg
/
/
*
/
/
1
Flue Draft
in. H?0
I
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I
NJ
I
-------
FUEL MEASUREMENTS
Date ^ - \ <, • S°1 Wood Heater Manufacturer_
Project No. Wood" Heater Model Sen
Run No. CT>
Circle One: Pretest Fuel • Test Fuel
Fuel Type and Amount 2x4 4x4 Ix4_
Ideal Load Weight ; Actual Load Weight ~
Fuel Piece Length .
Moisture Meter Calibration 12% 22'
ta/«.cc/ T<~,o. °F
Moisture Content-(Meter - Dry Basis)- CoivficTtd.
Readings Average
n s //.s
^ a
4
5 /Z^C 11A I2.V
6 /c,y / T..I
s /S-T y/.v i~).o
9
10
11 //^
12 .
13
14
15
16
17
18
19 _
20
Overall Fuel Moisture Average ll"l S
J-C-2-21
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run i
'-./&-ft 9*
ES Project }
'Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) ,"7-]"7 Thermostat Setting
Primary Air Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (eF)
Relative Humidity (5)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Pretest
2.1, 7 S
6.-&
^j c—
c
/OC//J-0'
/V/A-
Post Test |
Z/.& "2- • I
it 1
it- \
0 \
to.o/.a o 1
1
1
TEST FUEL DATA
to
Actual Fuel Charge Wt.
Coal Bed Range Wt. _
Actual Coal Bed Wt.
Fuel \\2°"' Dr~y lLJLL_Wet
Fuel: Dry Kg i ; • ~^
to
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Veloci ty Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
J-C-2-22
-------
HOOD IIEATEH CERTIFICATION TEST
TEMPEHATUUE AND PUEL CONSUMPTION DATA SHEET
ENGINEERIhJ.G-SCIENCE, INC.'
Cllunt ErH Run I
c-z-?-
Test Fuel Charge
. Page
Date K-/6»--$T Wood Heater Model SH3/Z Coal Bed
ES Project I
t-t
o
CO
Time
Sampling/
Clock
fiCjy«$
67V 5
oSv ^
Mv **>
'oH1^
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'^'Y.s'
/V^-r1?
1 «o H 5
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(-7 <-/«=>
/ 8 V^T
/ tyci
Test
;uel
Ibs)
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ft T_
t.7_
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foi£>
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03 Z.
.o'ZJ?
.01%
.^iz.
,6^0
jfj/lf
ifll 7
.CVS
'
Ab/2.1 Operators (dM,SKK
•
Comments
*l f. i s*i rt ^4 ti \s i'/ /) 9 11
• *J'\Pr 1 r\ ^* CJ V^^ r\J\ < ^ t^ *"l I'V'VlV*.
M T^*" i^^~CO3o -c^^ \f-&/I.Z. (?•(?" tfJfhl'f** Itio
/^J /, *//'7.5? - (^. V v/)l//>-.
/
1' ^ ^'o A A kp P7i c «^r r, /r
•
Coinl>ustor Temp.
"2J^3
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^bf/fi*
"7>vO
5S.fc>
3 55 2,-
c>'7 t>
5'c/"^,
T\~7f\
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"i%^
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•'i<> -7
?.-"'££?
Surface Temp.
lop
Hear
Dob torn
i~7ft
•Z^c-
•a-t'/
"ZCaff
"Z- c> 1
7 "2-3
•ZL.-V ^
"? C?2
7.0 C>
^07
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2-V
^.•S.b
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?;^-t^
/'^d
on.
Tun.
Temp .
Tf
?r?
?^7
9 *V
'ic.
%/
&S
9 "S
^•7
6V
g <'
_g<^
S "?•-
\ /
<^?o
Room.
Temp .
(itP
~l/
7/
rtS
^ ^
70
•/(j
~7'~s
-if
~)'o
~7o
7
-------
ENGINEERING-SCIENCE, INC.
Wood Heater 5 II ?> £-
Date j|-/f. - _
Sampling Location
Sample Type
Run Number C—^-'~
Operator
Ambient Temperatur'e
Barometric Pressure
Static Pressure, (Pj]T
Filter Number(s) ]
Meter if-- \,&H<-
SAMPLING DATA
Read and Record All Data Every
Start Time
Stop Time
dCf»-{5
Probe Length and Type
PI tot Tube Coefficient
Assumed Moisture V
Sample Box Number
Meter Box Number
Meter H
, ?•?
Pretest teTk Rate ,<3OZ.
Post Test Leak Rate .o^t/
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
D O&VS
/S
30
^
bo Q-?«5
1$
96
ID^
Ito OSSY*5
/•ill
/50
/£*
//K> 6?V5
/0-S
2^6
ZZ5
*yo /o«/5
355
0-7<3
iS5
3oO /^5"
^5
i>y$
~y-l*>,
1(eO nM*>
Gas Meter
Reading.
(\*> ft3
fo&fle?*.
^&3. /
<•
*7/0,3
,
7^0. .^
17
.050
• r.^)/
. OS/
,os/ __
,o « ?<'
.0^7-
i (\ R -? _
,O"S 7_
. 05> 2_
Orifice 1-
01 f fere
( H), 1n
Desired
« 55
^
ressure
ntlal
H?0
Actual
.ss
.55
rS^
.S^S
.•5^
rS^
.5-5
. 5?i
-5-5
,S'S
.f5«T
• 5'S
, -Ts'
*«~
' 5'T
..S'S
,?5
5S"
- SS
• 3' -5
v 6<;
.5^
, s^
. s s
•5--N.
TEMPERATURES
Dilution
Tunnel
Meter
In
(*&
90
y^
if
^{-L-
V
Filter
67
•
Impinger
5~a
77
S'c,
7^ ^"i
f^o •
5'-t-
7? 52.
75' 5-7
Pump
Vacuum
1n. Hg
t
1
/
/
/
/
/
Flue Draft
1n. H20
o
i
to
I
(O
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
JJJL,
Wood Heater
Date
5" -
^^ J(-«t- P >
Sampling Location_
Sample Type_
Run NumberJ
Operator /;
• "\ Clock Time
Sampl1ng\(24-hr
time, m1n\Clock)
^^7T— -Li&
•2,-)^ - s*>
-i,9o /^
•~/oS la
Vlo /'3V5
435
Lf5&
H^
V&& /^/uq
^?5
5/o
5'25
6V 0 I'5V S
^^
570
5? 5
Soo 1 ^ S
/'rf?
^>^>
^•^S'
160 ('/^'5
^7^
/,7o
ToS-
3as Meter
Read1ng3
S5e/. /
R8R^
9/6\3
9V7. 7
c)77.7.
Velocity
Head
UPS) 1n.
H?0
• c> c> o
.0^£>
oO*> O
.66"O
.<1S(
•0%O
,05o
.OS/
.65*0
.05-2.
.65 /
t\T /
«.S~
. S'S
• c> 5-
. s'S
, 5-5
.f?3-
-^ 5"
».^.C
..5'
.f?
- r.T
• 5T
, 35
. 5.S-
o f <-
' 5"^
TEMPERATURES
Dilution
Tunnel
Q.
i
^
-leter
In
•;*,
9-7
•51^
c/y
eio
Meter
Out
67
"Iz-
H/
•83
efa
Filter
sy
^?^'
-7f
^77
~>C1
Impinger
b<*
. a- 2_
5"?
6/
•
*l
Pump
Vacuum
In. Hg
1
/ •
/
/
/
Flue Draft
1n. H?0
•'
o
I
M
I
N>
en
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Uood Healer
Date //~/
Sampling Locatjon_
, Sample Type
Run Number_£
Operator AH
\. Clock Time
Sampl 1 ng"x(24-hr
time, mln^vClock)
^TS'c — tf'^£-
7?<3 -/ /^V^
7^^T 0>6
V/3 ~te
*z$ ->>&
ivo "la^
Gas Mater
Readi nq
(vm) ft3
/otx/-. y
/tf-5^.7
/035
Veloci ty
Head
(APS) 1"-
H,0
.r»f/
*<>$/
*oS/
*e>S/
"0^ /
< o T^
, C'.'S'O
, •« ^/
. 45 "2_
Ori f ice Pressure
Differential
(aH), -In. HzO
Jesi red
Actual
'• ^5
.-5?
6^)^
•*><$
' 5-T
. 5-5
, .5"5"
, 5'5
.5^?
TEMPERATURES
Dilution
Tunnel
i
..
leter
In
9Y •
<^/V
9i
-
Muter
Out
S %
« ^
87
Filter
7^
77
7C
Impinge'r
^/
SV .
srv
•
'ump
Vacuum
in. Hg
/
/
/
Flue Draft
in. H?0
>
I
o
-------
FUEL MEASUREMENTS
.(2-2-2
Date _ ([-
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f C-"2 -
ES Project i
"Wood Heater Model
Operators £.i_
5 /1 3 £T
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr) 1, I L/if
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft?) _
Fuel Charge Range Wt.
Pretest
Z/.^-j
A-l '
/V
O
A5.
-------
I
to
SO
HOOD IIEATEH CERTIFICATION TEST
TEMPEIIATUUE AND FUEL COHSUMPTIOM DATA SHEET
ENGINEERING-SCIENCE, INC.'
Client E P/l- Hun J
C-Z-
Test Fuel Charge
Page of _
Date ll'/7^S7 Wood Heater Model S/73/?. Coal Ded
ES Project |
Mine
Sampling/
Clock
A^3O
0 7 TO
0£>^\C>
O^l^r^
i6"3O
// 10
1? -2, O
I'S'iO
IM'SO
/
Iff ~*>O
ITho
(£"^o
/°Ko
•2(5^^
'
Test
ruel
Ibs)
}ife>
"^•L(
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3.J-
7, j'J
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5 T_
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%*'%
S /"-/
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Fl.ue
Draft
in •
1? 0)
rt^j^i
..
),0.£/^
0^&
0'38
931
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Q.Zfa
O.Lf5
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*d"52.
,^-^f,
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'.
fiJj/2 . *^_ Operators |/iV\\A
Comments
. ri.Z/.ft Z.t/^K.Xffl.-^f
^iV/Z-' *v 7.o * &«W«tf c:- r
oT(7- <-^>»'\
f.VAS 1,if^-Af.tc(f> cfi (•* t&yj
* »
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^^ s« S. e: ' w^-v«,
I^Z'Y - -1'irS.Q^- ^..O/T.^^ ?,£«
'
1
3>HcVv
1
Combustor Temp.
1 lo
(f\ Tb
cyoO
^c"7 Z_
St>/
-5 ^"2. •
766.
"//£>
T^t <7
170
6 7f <9
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Surface Temp.
lop
Hear
uottoin
\~L~L.
•
Z&7
737
T.'b/
y g •Jf'
/7 ^
'.?3
V6
u ^
o^--
(t°\
7V
6rS"
8 7_
^y
55?
61-5
Ip 1
9-7
Room.
Temp.
67
-? 7
vv
75
•5 V
G 7
S/> "7
-------
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
SAMPLING DATA
-•Z--3
• I "7
Sampling Location__
Sample Type ^ ^
Run Number £
Operator
C.
Start Time
Stop Time
Ambient Temperature^
Barometric Pressure
Static Pressure, (Ps)
Filter Number(s)
Meter y--
Probe Length and type
PI tot Tube Coefficient^
Assumed Moisture ~
Sample Box Number
Mater Box Number
Meter H
S
Pretest Leak Rate ,
Post Test Leak Rate
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
time.mln Clock)
O <%-3o
1*3
3
Ci^
6& 0730
7^
•v ' 0
/o^
/ 2 o O %"~3 ct
/35
/5o
/G>f>
/£>0 (3930
/75"
"*t Q
ZT-5
*T, I/ft • ^ ^ ^~'
2-*ys
~LT?O
-£Ql?
"%3O
~*><-f5
-7&0 f-^o
Gas Meter
*ead1 ng
fttn. fi'VA5
CfCl.^f
•
i to> « ^
4? V > )
/^(i- O
•2. / ^ . ^)
7.^-S-. S
Velocity
Head
( Ps),1n-
H?0
O.o^-^
6,030)
£). o Y ^
A6V 9,
6/^>&o
t).^5 2-
OrO1?;!-
,05 2-
»O5"O
, <^xS" £>
,05/
j O ^ 1
.0^'^
o^^Y
d fTS
, <"i .S" S
(J "j C-
» O ^ (j
. t>^' ^>
Orifice F
Differc
( H), in
Des1 red
, ^"i
ressure
ntlal
H?0
Actual
,55
.55'
i 'j-b
/ ^"S
.53
i.") "3
• 'SS
, 5 S
• "5 •$
• ''.S
. 5S
. 5" 5T
** ^ i
, <7<5~
' ^5"*?
5°^>
-sS
ss
, S.5"
,55"
. S"S'
. v-i
i ^> *?
•:? -s
TEMPERATURES
Dilution
Tunnel
Meter
In
o//
<-?•/
CA"/
<•!<-/
V7
$<• ?
"7 /
Meter
Out
^"7
07,
t?4-/ C'P ^
a 2. 5"?
5 7> • c', ? ..
7o f y
^
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
*
Wood Heater
Date
Sampling Location
Sample Type <$&-
Run Number C • i - 3
Operator
5-
• \Clock Time
Samp11ngX(24-hr
time, min\f,lock)
T&O — ,02^
T?r • /yc
*9o vv
Vc$ /^
V?c /^'Ji'
v?r V51
V^' , ^59
-v/,^ /c
V^o /V^o
^"5 V^
5/0 c»o
52-7 /?
5HO 1 5 3^>
5« V
dW n o
(MS • /T
i,(,o 1 -) 1o
fc75 VC
(1^7 i> /W)
705 /S
5as Mater
Reading.
(vm) ft3
Z7V. C
^04,T,
?3V.^
3^.?, 7
'^9 "5- *>
Velocity
Head
UPS) in.
H?0
ft,o^5
6.05 ^
A,0$Z,
0,^1^
«o5Z-
,c-5^
«o5^5
,6*?^
« 0 f^
^«5ry
.fP5S
««5r9
-dS--^
pr.f?
»OT2-
*0^3>
.c"T<9
/> oC5"
C
>5
TEMPERATURES
Dilution
Tunnel
•leter
In
8?
•>/
9V
<)3
93
-
Mater
Out
7S
ot
b?
«<-
^0
Filter
c?0
7ff
77
IS
7^
Implnge'r
& C
t
. rtf /
58
5v
•
<^a
Pump
Vacuum
in. Hg
(
i '
/
/
/
Flue Draft
in. H?0
I
o
I
10
U)
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
S
Hood lleater_
Date //-/-T^^.T
Sampling Location
Sample Type
Run Mumber__
Operator |
\Ai-t-
.}
\. Clock Time
Sampl 1 ng\(24-hr
time, mln^sClock)
/r-i'f"B — _____
-7^o / P,3o
T=75
•75'°
-765
-75b ^3-0
7 ^C Vr
_37o «r'r.
^29 75-
XVo ^O^o
Gas Meter
Readi nq
(y,^
^^A
V3/.Z76
Velocity
Head
UPS) ^.
ll?0
AflSV
.o.^-V
. ^.-5t.
«0?7,
* (?5~o
o 0 T'2_
,0^/
.033
,&$•/
Orl fice Pressure
Differential
(fill), -in. H?0
Desi red
Actual
,•55
:5~5~
..->S
'?f
«^
p5-^
TEMPERATURES
Dilution
Tunnel
i
Hater
In
•7V •
TV
Filter
"76
vs
77
Implnge'r
X^
<& / .
^'6
•
.
Pump
Vacuum
1n. Hg
/
^
-2_
Flue Draft
in. H?0
-------
FUEL MEASUREMENTS
-
Date _ i- /"C ' Wood Heater Manufacturer
Project No. x V\ I. Z 3-» Woocf Heater Model S
Run No. C-"L-"H _
Circle One: Pretest Fuel • Test Fuel
Fuel Type and Amount 2x4 _ 4x4 1x4
Idea] Load Weight • .ActuaT
• Fuel Piece Length
Moisture Meter Calibration 125
u/«,oW T*~,v. "I-
Moisture Content- (Meter - Dry
Piece No. Readings
2 //,/ /'«2- ll'l
Load Weight
225 '2 ^ ' /
Basis)-c°'*''Cl II.S 11$
7 . '3,c/ /3,& ^.3
8 A/c ° //.7 /a,? //.g
10 /6,6 /'JS.-^ Ze/i
11 3Z,y -^2,y y»,/
12 ^' 3'/..2 ?1A. .?/'$"
1 ^Si!;!'
15 /s.5" /o,9 /o,^O
J-C-2-33
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run t r> ?:
ES Project }
l"Z- S
"Wood Heater Model Sl7
Operators LO rt [4 , ,_
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr) |. \ ~Uj; Thermostat Setting
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (S)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Actual Fuel Charge Wt.
Pretest
Z/,~7~7
7-Z-
i <=;
*£> (** ' 1 ^ (*i
/C,&'(t£f-*,
/\)>V
Post Test
•^/"VC:
&
/
-------
ENGINEERING-SCIENCE, INC."
Client EPA Hun I
WOOD IIEATEH CEIlTIFtCATlON TEST
TEMPEUATUIIE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
. Page
.r
Date ((.- 10 "M^?^ Wood Heater Model <^>l~l'?tf- Coal Ocd
ES Project f
i
n
to
i
U)
'line
Sampling/
Clock
fifi n o
o c/txy
/ crtrt,
lloo
\1&&
I "^u-tt
f'/fO
I'y&o
flttrb
'/"7 im
I'ntrO
tiro
Test
:uel
n.
IDS)
\(r
9,4>
/£.y
i'1^
3,L
£, 6
"?«• 5
2.. ^
•? «y
11 ,v
7'tf
'Z • £
Fl,ue
Draft
in
i.OI B
*•
o,Ci%
»b3¥
G72-5
oZZ-
^»'7^
d?.y^
t^.'i^
nC^
*rt//V
,!/»'? 2-
^>tf^^
t^~l
•
'.
... • - i — -
K^(7lJb Operators 60 tl ^ . V\KCI^
.
Comments • ,
,6* t/l>(0 Htte** Krvlfr-r &(J(fv X*V« ft f\f 0 "^" Oc^n-^." /' (^ ^?^t*
"ti^^^ '^irr~ SC~V" C^. V\/C <^s t
(
' "5"^* C» ? * ^*X "T4 H* "* ^ / ^* /^'^ X
/^5 ?n y«fr*^X /*/ 'X''1 /? //> ^ CyT" ^ ^*
/& T~) fat* 77» /M y^J .
7^ /flVf /3 /'/i 7>» y^t /ix
•
/
Combustor Temp.
~Z_"^ "2_
.^'H^y
5" ~\ 9
— a,5"cj
Tto/
"? £» ** •
7Z3
^i *^ -T^
*"J *2 ^"
"7 ^ ¥
V£ "Z-
5"y s'
3
l&f
/ ^3
"^.y?
^37
17 6
'a. /o
3 0 %"
1(1 glit
Teft
•
Stack
Temp .
Fj(.j
37?
^?VZ
2-S-/
'ZV7
y^T.
'??•;
4/-^<^
2*)"z,
"?^7
"5"^/
on.
Tun.
Temp .
-7 7
&*/
^S'
f3£i
ff3!
B?
91-7
9^,
9 £
TV
-
Room.
Temp.
&*?
(f(-
(*~S
4 7
^V
-------
ENGSNEERING-SCIENCE, INC.
Wood Heater_
Date II
SAMPLING DATA
Sampling Location
Sample Type V\S <=i
Run Number
/S
if-^
<^>
'TS
7O
/D-S
1 2jO (&OO
/3S
('SO
1 tef^y
/ *-?& ) t *->^~*
/?$
2i&
72.^
•ZHo 1 Zoo
2.^
->-!&
^QC,
-y^3 i"^,oO
~v^
Tiiu
-^Y^
-Vi^ / ^/c-O
Gas Meter
Reading
(VJ ft3
^ n Vl CAfl
5/Z 6»
6
^>y/f G
«
^70, «
/i ££>. "2_
^Z9. S1
0>^5 1
(0, o*Sci
t'iD'oD
6-09-0
/l,^1^ /
^flfo
, of/
a 0 <^1—
t Ot'L
•L&C-> Z=-
i ^ S" t)
, OS °
i^^O
, oSO
,0^0
. C''?"?
^ d *»"/
4o^~o
* O'-tO
* aJ?CJ
ff n 5°
. o^'o
Orifice ^
Dlffere
( H), 1n
Desired
.•o.5"
'ressure
:nt1al
H?0
Actual
,S"5
^•^
i ^~> ?
c^
/ 'S'S
,•55
/ S
f-$5
*•*•>$
<£>Y>
• 'j""s
, r; T
• 55
,*5S
35
• 5" "^
o ^"'T
v 5X"
.TT
' $5~
-5T
/» * j
^•:S"5"
^5"S"
TEMPERATURES
Dilution
Tunnel
Meter
In
£L/
AS
tf 1
•^ /
7V
tfb
CJII
Meter
Out
^- LI
Implnger
(e ~~Z—
7-fT ^ s
9*7
97
7-5' «To
77 • .-S-Ji
P*^ 5 *>
72 5"c
Pump
Vacuum
In. Hg
f
^
/
/
/
1
/
Flue Draft
1n, H20
-------
SAMPLING DATA (cont.)
Wood Heater
ENGINEERING-SCIENCE, INC..
Date //-/§ - SI /
Sampling Locati
Sample Type 5~<
on Crpi^ed /^t-7y^
Run Number j£ - 2 ~Y
Operator Jtif/3 * J /V •
t_
I
0
i
ro
I
OJ
i
• \Clock Time
Sampl1ng\(24-hr
time, min \Clock)
36 ^ — " 13-&L.
^"75" • JS
"39° lo
Yo'y LfS~
LJ2.6 ' 1 *J0D
£J~l ^C i ^*
• ^O* *^ ^|
y^5" V5~
VS^ /"^ <^o
4/9f /T
5/o 3
5~cj /
* o ft?
+ C>V$
eO'i'S
+ /TV "7
,«'/<}
u (J^O
• c>
• o*5o
fO 5"c*
,,050
/.^>T/
^) ^ O
rf /7 S^C>
* £? j O
* & 5~/
o O So
f o So
Orifice Pressure
Differential
(AH), -in. H?0 '
Desired
Actual
, e^
-------
FUEL MEASUREMENTS
Date ll-lQ-S0! Wood Heater Manufacturer Hc-o^y \
Project No. K Tj|2?) Woocf Heater Model S ( "73 ^
Run No. ("'--?.--<.'/
Circle One: Pretest Fuel Test Fuel
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; _.Actual Load Weight
-Fuel Piece Length .
Moisture Meter Calibration 12", 225 1L~1 , I
Moisture Content-(Meter - Dry Basis}—
Piece No. Readings Average
1 ^ 27JU3V£_ Z5<7
2 !(£_/«£_ ti'8
4 ° )/,£> J/J j/.$
5 /^_6 JK2.J5,1.
6 ;v.i
8 /A£
9 //,
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
• •' Run f C-
19-
ES Project I K f\ \ 1 j
'Wood Heater Model
Operators /.
S / 1 3 £
\Hf (Q
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) C\ £"70 Thermostat Setting
Primary Air Setting • Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (*F)
Cold Draft
Firebox Volume (ft-)
Pretest
T./.9&-
- a
0
/O.C//&-0
MA
Post Test
•Z /. 9 / •
/•5
&
/*.*>//£>• '0
TEST FUEL DATA
Fuel Charge Range Wt. _
Actual Fuel Charge Wt.
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H20% Dry ('U'O
Fuel: Dry Kg f Q,
to
Wet
LOADING/TEST START OPERATIONS
By-pass Air Settings
Door Comments
Velocity Traverse
Temp
A 1
2
3
4
B 1
2
3
4
Ave.
Pitot Leak Check
Static
J-C-2-39
-------
C-z-S
WOOD IIEATEK CERTIFICATION TEST
— .
v_E?
a»«™
Wr«J)
TEMPERATURE AND FUEL CONSUMPTION
ENGINEERING-SCIENCE, INC. „ _, ,-
CHunt eP/3 Run/ C '«-'-> Test Fuel
Date
J/-/9-* Si ^ Hood Heater Model 3n3lI5 Coal Oed
ES Project I
I
o
I
0
Mine
Sampling/
Clock
ORxSc)
^y^oo
//7
/(^> r\
j-^oo
/"^>c>o
IH^O
i&O
l(j>()O
l^/oO
IfxT;
C^crO
2A5O
Test
ruel
n.
Ibs)
/i Z-
5'ift
*• ' /^
•2.^0
i <*
/o,o
t?. 2-
5"( 2.
"3>.c>
•7,^9^
i^-i.
ft fa
l.t
Fl.ue
Draft
l"n
.O/O
O.OSO
d^£>
OT.'i,
iD.2I^>
O^A
o;Z3
O"32>
0^2-
OTta
nUQ
(> x*^
ozft
-.
Operators i^U.tA
Comments /,
V'6//. Z— 3-Cs1* ki'vl(,^« Ocff.loet'
fi. (S-O*4- Cldd^'Jl &,£>&')~1
Oir .Sc'i^ ivv^x-
c)3zZ- - ar <^,<>-t c^> "^v-v^
/j
/ 3,6 //^ //. &<*<.*<*** e /rvo
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~2J-i~7
^l 7
"^-7 / •
'S'v^
7\C-S
M"s?i
t/<7'Z-
•?s (
DATA SHEET
Charge 6- '' (
Surface Temp.
lop
Hear
Dot torn
( Z/}
•
~iif-/
~2-~2. ~*>
'<$*
l~7
">.**> f>
__ of
on.
Tun .
Temp .
~7/
/OV
£>??
ffA
&f
?0
o1?
9/
9V
/o "^
Q y
Ci — 7
(T ^
Room.
Temp.
6^
67
~j /
73
^7 -^
6^
f^°)
~i &,
-)<4
-) y
7o
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date U
C-Z.-S
SAMPLING DATA
—yy^-A
Sampling Location
Sample Type_
Run Number
Operator
Ambient Temperature^
Barometric Pressure
Static Pressure,
Filter Number(s)
Meter Y "•
C.R
Start Time
Stop Time
£80-0
Probe Length and Type_
Pi tot Tube Coefficient
Assumed Moisture tf
Sample Box Number
Meter Box Number
Meter H
Pretest Leak Rate fl.QQt-f
Post Test Leak Rate Q.,CSC> 7
le
Read and Record All Data Every
Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
/•s 0&C6
y/5
^e>
ift$
4,0 Q'ioC)
7^
*?£>
105
iTt1^
/f\ 1 1£*&
/"*•?*-!
?/£>
t2£,
£t/C) d^o
Irt^
•ZT70
•2X5
7&L> nV5
9^0 /^^>Ci
Gas Meter
Reading
(VJ ft3
G
'^fofa *tl
*&?/> 3>
,
92-^. (
953.^
C\£)i. ~*>
16 tl i(j>
Vel oc1 ty
Head
( Ps).1n.
H?0
6. OS'S
.£>%'"/
,655
.053
, ^j^ -^
. ^^ "?
, 05 s
-OS'S
.065
•» /i 5 ^l'
. O*>"<£»
.CS'C
0^" (2«
O^G*
,05^.
,05'^
. 5 V
, (Di'v' "J> •
.OSS
j£>
• O5 6?
, <^>SfT
•
Implnger
4 O
7ti ^^
? 5" "T^
7^ S^-
(f?^-- 5^
SJZ. ^
-------
SAMPLING DATA (cont.)
cgnr-n VSrUttf
ENGINEERING-SCIENCE, INC.
Vlood Heater S l"7 3 f^-
Date
//- I'l-ftf?
Sampling Location C ^>
Sample Type
f^£j
Run Number £.'-?.—£!>
Operator A if//-( , -SMcf^
t-c
1
o
1
NJ
1
.p-
N>
\. Clock Time
Sampl1ng\(24-hr
time, min\f,lock)
~ ~ .
~?>"7 s"
'3i *-"*
^•/o^
*-/Z£> f *$'£>£>
*i"2>5
^^"o
^^
/JQC) /(;£> O
LY^
<=>/£<
^2-^"
^o ilof>
t->l3C:>
E)7D
JS85
d*?® /ft&O
bf?
f-ID
//>v>
/^•^ (°ID&
0>1h
(r£)C>
Jt>5
Gas Meter
Readi ng
G>y&. ti"
|O /0,O
O^^v I
//?ff.3
II Citt t 1
Velocity
Head
UPS) in.
H?0
Ao5"^i
. £>%5
\O SS
;, "3V
_j_£>cj 3
. OS'S
.05?
.°5'Z-
. o "p ^
a O^ 3
« (7^>~i.
t O S 2.
« o5"7_
« S~
, .5" ^>
''T'T
• ?S"
• <5'
-------
FUEL MEASUREMENTS
Date II- C9-R cf Wood Heater Manufacturer
Project No. }% t\ ( ? "^ Wood" Heater Model <
Run No. r" -'->-<: ~
Circle One: Pretest Fuel /Test Fyel
Fuel Type and Amount 2x4 4x4 1x4
Ideal Load Weight ; .Actual Load Weight ~
Fuel Piece Length
Moisture Meter Calibration 12% ' 22% 7_'
Moisture Content-(Meter - Dry Basis)- Corvec7t
3 /O /£./ /^/ '
4 . /6,L_ /S7_ _/f^
6 /9,c/ IcJ /^. ^ .
7 /5.6 /6,o J5,£
973^ E^-S_Z1G_ ZZ.7
10 f^ r]i_ rte
11 2.5.tf z.2.(.' 23,3
12 l.b±
13
14
15
16
17
18
19
20
Overall .Fuel Moisture Average
J-C-2-43
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
. /•> . • ->
Run t
U - 2.0
ES Project f
,
"Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Secondary Air Setting
Achieved Burn Rate (Kg/hr) ^^1SH Thermostat Setting_
Primary Air Setting Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (9F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft?) _
Fuel Charge Range Wt.
Pretest
Z /. '? O
/o
£>
/6\
-------
c-z-c.
ENGINEERING-SCIENCE, INC.'
Client BRA Run I
WOOD HEATER CEHTiriCATIOH TEST
TEMPEUATUUE AND FUEL COHSUHPT10H DATA SHEET
Test Fuel Charge
Date
ES Project I
X £> /ft
y*i?>
-7 V.I
6 X "3
•35% y
q2 z
V/<^
-!.*;/;
-2 a/
Surface Temp.
lop
Dear
Uottoiu
/Z2-
/6V-
T?c.c>
-2. "4 "2.
/^ 7
-2-67
Z30
ToS
n t
Right
Left
•
Stack
Temp .
K/
-Vo
<•//•-/
^<^
7<^
•7^
11
•?
-------
ENGINEERING-SCIENCE, INC.
Wood Heater S |1 3 E-
Date il--L"->^q
SAMPLING DATA
Sampling Location
Sample Type_ 5'"
Run Number
Operator
Start Time
Stop Time
c.
C - 3 -
Ambient Temperature]_
Barometric Pressure
Static Pressure, (PjJ
Filter Number(s)
Meter Y-
Probe Length and fype
Pi tot Tube Coefficient^
Assumed Moisture ]
Sample Uox Number
Meter Box Number
Meter H
ft/-'
Pretest Leak Rate
Post Test Leak Rate
•J ,00 -5
Read and Record All Data Every GO Minutes
Clock Time
Sampling (24-hr
t1me,m1n Clock)
0 0-7^3
i /o9 ^f ^
/35
/5C.
/elO 16 *V 6'
/•r'5
2/e>
7^S
ZVo | ( *y ^
7.55
2.7O
•^CJC,
Ifio ( IV"?
•^15
'33o
Gas Meter
Reading
/fiv.7oy
^/5>' ^
,
~24'&.'5
7.71? •*/
^o V * 5^
1, "^ "?7 , ^
Velocity
Head
( Ps)Jn.
H?0
A. oS5
6-09-i
.65 3
(d'o V
t<35V
i <^5'i
.(^S'" IL
^65 Y
, OS-'f
,^5v
• ^ 5 T>
/i <3 f£3
oO $' 3
, (5^5 "l>
e O*?*-/
— /"• ^y
i o 52.
* <;/
Orifice 1
Dlffere
( H), In
Desired
'"rff
ressure
:nt1al
H?0
Actual
.
* j S
<. 5"*9"
eSl^
J!*?"^
.> 5" 5^
- •T-r
TEMPERATURES
Dilution
Tunnel
Meter
In
•76
?n
c(c^
99
99
/&?}
Meter
L_PJ^L
^9
&G
£) K
<32,
Vv
9y
Filter
^.X1
Implnger
<^>^
-76-
V "7
t~^
f?f/ 55' 2_
5'
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Oate ft'
Sampling Location_
Sample Type_
Run Number^;
Operator /-t-t
- "2 -
• "X. Clock Time
Sampl1ng\|24-hr
time, mlnXJJlock)
"^i£~6 ~-i2t^S__
'^7^ • cso
34* /5^-
^^>5?,
. CJ f5-Z
.o5*Z_
* o 5V
- r-"5~Z
. tf'^Z
Orifice Pressure
Differential
(all), -In. H?0 "
Desired
Actual
-jCC
^^r
. 5«r
.$T
«$"5~
• ^5"
.55"
• 5-r
TEMPERATURES
Dilution
Tunnel
later
In
?7
^S
-
Muter
Out
<5/
9/
Filter
^6
»
-------
FUEL MEASUREMENTS
Date //-?-O-$b'7 Mood Heater Manufacturer /4
Project No. RD iz~^ _ Hoo
-------
TEST SERIES
C-3
-------
I
O
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: HflUGH'S PRODUCTS Units l=»etric,
Model no: S173E 2:£nglish:
Lab name: ES/CB Y, 0611:
Tst date: 11-28-89 Pilot co:
Run no : C-3-1 Gas MM :
Tst time Pb (mm, in. Hg):
(min): 600.00 Tunnel area (m2,Ft2):
Chrg ut Wood moist (X uet):
(Ib uet): 33.80 Burn
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
vel dp
(mm H20)
(in.H20)
0.056
0.050
0.049
0.051
0.051
0.049
0.047
0.048
0.048
0.048
0.047
tunnel
temp
(C.F)
55
88
105
75
73
91
115
91
87
82
82
DGM
rdg
(m3,ft3)
441.912
471.100
500.500
530.000
559.500
589. 100
618.400
648. 100
677.600
707.200
737.778
0611
temp
(C.F)
50
65
73
75
71
78
82
85
84
85
85
Samp vol
2 (smS.scf)
1.046 223.613
0.99
28.56 Flou rate
21.86 (dsmSm.dscfm)
0.1963 140.49
12.61
rate (dry kg/hr): 1.34
OGM dH
(mm H20)
(in.H20)
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
vel
(m/n
iin)
PR
(ft/min) (.?.)
1091.
1063.
1069.
1061.
1059.
1056.
1056.
1045.
1041.
1036.
1025.
43
83
35
60
61
02
53
19
39
62
76
100.
103.
96.
96.
101.
103.
99.
99.
98.
102.
4
9
7
7
3
6
8
0
9
5
dOGH
vol std
(m3,ft3)
23. 127
22.629
22.365
22.282
22.526
22.007
22.143
21.873
21.988
22.672
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel OGM
ave temp ave temp
(C,F) (C,F)
0.01 1055.21 85.82 75.73
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
O
I
u>
I
N>
Stv manu:
Model no:
Lab name:
1st date:
Run no ;
1st time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
IK)
240
300
360
120
480
540
600
HflUGH'S PRODUCTS Units l=metric,
S173E 2=English:
ES/CB Y, 0611:
11-29-89 Pilot co:
C-3-2 Gas MU s
Pb (mm, in. Hg):
600.00 Tunnel area («.2,ft2)s
Hood moist C/. uet):
26.60 Burn
vel dp
(mm H20)
(in.H20)
0.060
0.056
0.059
0.060
0.061
0.059
0.061
0.061
0.055
0.060
0.057
tunnel
temp
(C,F)
74
110
86
86
84
95
93
88
132
107
96
DGM
rdg
(m3,ft3)
739. 8H
769.400
798.500
828. 100
857.500
886. 900
916.200
945.800
975.300
1004.700
1034.340
DGM
temp
(C,F)
65
77
83
87
88
89
91
90
91
92
91
Samp vol
2 (smS.scf)
1.046 218.405
0.99
28.56 Flou rate
21.87 (dsm3m,dscfm)
0.1963 152.17
9.55
rate (dry kg/hr): 1.09
DGH dH
(mm H20)
(in.H20)
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
vel
(m/min)
(ft/rain)
1150.12
1147.97
1153.24
1162.97
1170.48
1162.71
1180.12
1174.77
1159.42
1185.13
1143.86
PR
(.?.)
108.
99.
100.
97.
98.
98.
96.
104.
101.
97.
2
9
0
4
6
3
6
7
1
6
85.49
17.640
460.00
1850.00
dDGH
vol
(m3,
22.
21.
22.
21.
21.
21.
21.
21.
21.
21.
std
ft3)
783
908
038
729
689
576
718
684
571
708
vs/VmTs vs ave tunnel DGH
ave temp ave temp
(C,F) (C,F)
0.01 1162.80 95.55 85.82
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
O
I
CO
I
CO
Stv oianu: HflUGH'S PRODUCTS Units l=metric,
Model nos S173E 2=English:
Lab name: ES/CB Y, OGM:
1st date: 11-30-89 Pitot co:
Run no : C-3-3 Gas MM :
1st time Pb (mm, in. Hg):
(win): 600.00 Tunnel area (m2,ft2):
Chrg ut Wood moist (7. yet):
(Ib uet): 34.80 Burn
run
time
(min)
0
60
120
180
210
270
330
390
150
510
570
600
vel dp
(mm H20)
(in.H20)
0.(M6
0.042
0.013
0.043
0.043
0.042
0.043
0.044
0.044
0.042
0.043
0.044
tunnel
temp
(C,F)
85
115
1H
100
96
117
97
100
90
135
89
87
DGM
rdg
(m3,
35.
65.
93.
123.
139.
169.
197.
227.
256.
282.
309.
324.
ft3)
232
200
900
500
300
100
900
100
700
900
700
543
DGM
temp
(C,F)
63
76
85
87
78
86
89
93
91
89
86
86
Samp vol
2 (sm3,scf)
1.046 214.372
0.99
28.56 Flou rate
21.78 (dsm3m,dscfm)
0.1963 129.27
9.31
rate (dry kg/hr): 1.43
OGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
550
vel
(m/min)
(ft/min)
1019.46
1000.58
1011.54
999. 13
995.56
1002.32
996.45
1010.68
1001.62
1017.83
989.27
998.88
PR
GO
108.4
103.0
100.8
107.8
107.7
98.3
100.2
97.7
94.7
88.3
100. 8
dOGH
vol std
(m3,ft3)
23.070
21.558
21.867
11.630
22.301
21.237
21.414
21.551
19.144
19.654
10.945
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1003.61 102.08 84.08
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
o
I
u>
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
HRUGH'S PRODUCTS Units l=metric,
S173E 2=English:
ES/CB V, D6M:
12-1-89 Pilot co:
C-3-4 Gas HU :
Pb (mm, in. Hg):
600.00 Tunnel area (m2,ft2):
Hood moist (.'/. uet):
25.20 Burn
vel dp
(mm H20)
(in.H20)
0.048
0.046
0.046
0.048
0.046
0.048
0.048
0.050
0.050
0.047
0.047
tunnel
temp
(C,F)
75
100
92
86
95
85
84
84
79
105
98
DGH
rdg
(
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
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I
Ui
Stv «anu: HflUGH'S PRODUCTS Units 1-metric,
Model no: S173E ^English:
Lab name: ES/CB Y, DGM:
Tst date: 12-2-89 Pitot co:
Run no : C-3-5 6as MU :
Tst time Pb (mm, in. Hg):
(min): 600.00 Tunnel area (m2,ft2):
Chrg ut Hood moist (.?. uet):
(Ib uet): 29.00 Burn
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
vel dp
(mm H20)
(in.H20)
0.046
0.047
0.047
0.047
0.048
0.048
0.049
0.049
0.047
0.047
0.047
tunnel
temp
(C,F)
69
88
105
102
98
94
86
85
110
115
105
0611
rdg
(m3,ft3)
623. 102
652.700
681.700
710.800
739.800
768.900
798.000
827.500
857.000
886.400
915.983
DGM
temp
(C,F)
62
71
79
83
87
90
90
89
87
90
94
Samp vol
2 (smS.scf)
1.046 219.096
0.99
28.56 Flou rate
21.96 (dsm3m,dscfm)
0.1963 136.72
11.39
rate (dry kg/hr): 1.17
DGM dH
(ma H20)
(in.H20)
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
0.550
vel
(m/fflin)
(ft/min)
1000.26
1029.07
1044.91
1042.13
1049.41
1045.64
1048.82
1047.86
1049.53
1054.12
1044.91
PR
GO
107.
104.
100.
99.
97.
95.
96.
101.
102.
100.
8
1
8
2
5
9
7
4
2
0
85.49
17.640
460.00
1850.00
dDGM
vol
(iti3,
23.
22.
21.
21.
21.
21.
21.
21.
21.
21.
std
ft3)
017
170
916
680
596
478
773
813
818
834
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C.F) (C,F)
0.01 1041.51 96.09 83.82
'
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
O
I
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
HRUGH'S PRODUCTS Units l-metric,
S173E 2-English:
ES/CB Y, OGM:
12-3-89 Pitot co:
C-3-6 Gas MW :
Pb (mm, in. Hg):
600.00 Tunnel area (m2,ft2):
Wood moist (.?. net):
23.20 Burn
vel dp
(mm H20)
(in.H20)
0.046
0.047
0.047
0.047
0.048
0.048
0.049
0.049
0.047
0.047
0.047
tunnel
temp
(C,F)
71
72
94
97
100
85
82
81
93
90
86
(n,3
916
946
976
1004
1034
1063
1092
1121
1150
1180
1209
06(1
rdg
,ft3)
.923
.700
.400
.800
.000
.200
.300
.400
.700
.300
.983
OGM
temp
(C,F)
67
75
83
86
89
90
87
87
86
88
89
Samp vol
2 (sm3,scf)
1.046 218.618
0.99
28.56 Flou rate
21.94 (dsmSm.dscfffl)
0.1963 137.87
12.19
rate (dry kg/hr): 0.92
DGI1 dH
(mm
(in
0
0
0
0
0
0
0
0
0
0
0
H20)
.H20)
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
.550
vel
(m/min)
(ft/min)
1002.61
1014.40
1035.16
1037.96
1051.77
1037.58
1045.45
1044.48
1034.23
1031.42
1027.66
PR
m
105.1
106.3
98.7
101.2
96.7
96.9
96.5
99.5
101.1
100.6
dDGH
vol std
(m3,ft3)
22.916
22.515
21.212
21.690
21.571
21.458
21.576
21.724
21.987
21.968
85.49
17.640
460.00
1850.00
vs/VmTs vs ave tunnel DGM
ave temp ave temp
(C,F) (C,F)
0.01 1032.97 86.45 84.27
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: HflUGH'S PRODUCTS Units l=metric,
Model no: S173E 2=English:
Lab name: ES/CB Y, DGM:
Tst date: 11-28-89 Pitot co:
Run no : C-3-7 Gas MM :
Tst time Pb (mm, in. Hg):
(min): 600.00 Tunnel area (m2,ft2):
Chrg ut Mood moist ('/. uet):
(Ib uet): 23.70 Burn
run
time
(min)
0
60
120
180
210
300
360
120
180
510
600
vel dp
(mm H20)
(in.H20)
0.050
0.012
0.012
0.050
0.051
0.050
0.050
0.050
0.051
0.013
0.050
tunnel
temp
(C,F)
68
too
92
96
88
86
83
88
87
1 18
106
DGM
rdg
(m3,ft3)
210.902
210.900
270.000
298.800
327.800
357.000
386.300
115.700
115.000
171.800
501.592
DGM
temp
(C,F)
63
75
81
86
88
89
90
90
93
90
86
Samp vol
2 (sm3,scf)
1.016 217.126
0.99
28.56 Flou rate
21.80 (dsm3m,dscfa)
0.1963 138.21
8.56
rate (dry kg/hr): 0.98
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
550
550
550
550
550
550
550
550
550
550
550
vel
(m/min)
(ft/min)
1015.67
986.99
979.92
1073.01
1075.89
1063.35
1060.12
1065.29
1071.91
1071.96
1082.65
PR
CO
108.6
107.5
106.8
95.9
95.6
96.3
97.6
96. 7
102.1
lOl.l
85.19
17.610
160.00
1850.00
dDGM
vol
(03,
23.
21.
21.
21.
21.
21.
21.
21.
21.
21.
std
ft3)
111
920
153
101
173
507
512
168
716
829
vs/vmTs vs ave tunnel DGM
ave temp ave temp
(C.F) (C.F)
0.01 1052.71 92.00 81.61
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED // - ~2 5 - % c
DATE RETRIEVED
TEST LOCATION C~flf><7f>(-S ft,. 9
Q t n "j "7
X~ SAMPLER SN# " 0> {_ t-d.
(HG BAROMETER UNCORRECTED)
PRETEST B.P 31. 8~7 (IN HG)
TANK Z./.SS (—IN HG)
TORR ABSOLUTE • ^ I
POSTTEST B.P. "L/^5'^ (IN
S.5c
$, S$ TANK //«.*"/ (IN H80) FINAL 6 • 1 (IN H20) LEAK RATE .-
(IN H20 MIN)
POSTTEST LEAK CHECK
START C , °L (IN H20) FINAL^ . g (IS H2) LEAK RATE<^«
(IN H20 MIN)
POSTTEST GAS ANALYSIS
C02 (Z)
RUN COMMENTS:
CO(Z)
02 (Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN. -!- MIN. + MIN. + MIN. . DELTA
J-C-3-8
-------
CLIENT
ES PROJECT A ft / 2 3
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No. ^tOPl-Cr'**-/ Placed in Dessicator: .Date/TimeJAjlHSL!
STOVE MODEL No./46?^/4.? 5 5-/?3~£
POSTEST
1
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WT 2,
. WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
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PARTICULATE WEIGHTS SUMMARY Page of.
RUN Mo. (JrH-C'^> Placed in Dessicator: Date/Time.
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POSTEST
Acetone Lot (t.
Acetone Sample Volume.
WT 1
WT 2 .
WT 3
WT 4 -
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PRESSURE
Initials
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-------
PARTICIPATE HEIGHTS SUMMARY
Paye.
_of.
CLIENT
RUN No. C ~3 " / Placed in Dessicator: Date/Time.
3
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STOVE MODEL No.
POSTEST
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Acetone Sample Volurne__9_ZJL
77
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77. ^(i.7l9
77. 1670
•77./f^3
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• CALIBRATION WT
WT AMOUNT =
PRE WT
5e> • , ooaO
ROOM CONDITIONS
RELATIVE
HUMIDITY
/2&7/.
l%© ~7o
BAROMTRC
PRESSURE
•
Initials
Aie-#
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(BLANK CONG.) x
(ACETONE SAMPLE)
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TOTAL PARTICULATE CATCH (A+B+C) =
me.
-------
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PARTICIPATE WEIGHTS SUMMARY Page
RUN No.^r-3"/ Placed in Dessicator:
STOVE MODEL No. ///I*-*) k < 5 5
POSTEST
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//- 2^-57
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TARE WT
WT GAINED
DATE /TIME
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BAROMTRC
PRESSURE
11. r
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Initials
1
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(A)
.(B)
-------
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ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Paga / of /_
RUN No. C"^" ^ Placed in ' Uessicator: Dai-e/Tiine_ih_l
STOVE MODEL No.
POSTEST
L
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' WT 1
WT 2
. WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
(Z-l (5>/Z2$
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WT AMOUNT =
PRE WT
j» *> <>0l>
t> ^Crc>&
POST WT.
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srW?^
ROOM CONDITIONS
RELATIVE
HUMIDITY
_!<& @>67
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BAROMTRC
PRESSURE
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CLIENT ,
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PARTICULATE WEIGHTS SUMMARY Page of
RUN No.
-------
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PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT
RUN No. ®iv*o
j*—
ll-VW (c>^
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BACK
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*> & ~7 ^- (o
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CALIBRATION WT.
WT AMOUNT =
PRE WT
, $~*c.
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ROOM CONDITIONS
RELATIVE
HUMIDITY
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^O7/
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PRESSURE
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2A S
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(B)
-------
PARTICULATE WEIGHTS SUMMARY
of.
CLIENT
ES PROJECT
RUN No. d" •$'" 5> Placed in Dessicator: Date/Time,
H Q )2. 3 STOVE MODEL No. M"? <~c
s
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POSTEST
1
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WT 2
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FINAL WT
TARE WT
WT GAINED
DATE /TIME
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ROOM CONDITIONS
RELATIVE
HUMIDITY
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-------
CH
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PARTICULATE WEIGHTS SUMMARY Page
RUN No. Placed in Dessicaior:
STOVE MODEL No.
POSTEST
of.
2'z-
1
1 WT 1
WT 2
WT 3
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FINAL WT
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-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Pace. _ _of _
RUN Ho. C~ ^"7 Placed in Dessicator: Date/Tims 17, - ?- *? *7
rfs &•
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STOVE MODEL Mo.
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WT 2
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WT AMOUNT =
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. <$ ou 1
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ROOM CONDITIONS
RELATIVE
HUMIDITY
/*-(£)?/
J_l
-------
Client _
Date // - Z S
WOOD HEATER CERTIFICATION TEST INFORMATION
/yft" '_ Run I 'C ~'3 ~ /
ES Project
/Z
Wood Heater Model
Operators /ft f A
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) Secondary Air Setting
Achieved Burn Rate (Kg/hr) I , 3U/0 Thermostat Setting
Other Settings
Primary Air Setting
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (?)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (CF)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
~Li . S"?_
<97
/ £
0
/D,O//C, o
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Post
'*-/.
Test
5^7 •
G 7
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ENGINEERING-SCIENCE, INC.
CHunt t^PARun
Date //-IS - °6 °I Wood Heater Model /Ai^Ks- 5
ES Project #
'line
Sampling/
Clock.
lOl^ti
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\ ^7 (rv
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/^ 0~t,)
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t~ 1 c^>
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Comments
.T C CA ^c /#'
f}/i~ Ai'» 7° />M<. A' ~>u "'/^
/
Conibu
^.
V
6 -
1
V
6
^
7
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3
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HOOD HEATER CERTIFICATION TEST
TEMPEHATUUE AMU FUEL CONSUMPTION OATA SHEET
Test Tuel Charge
Page / of
<~ I
)' Coal Bed
Coinbustor Temp .
VC-
V7
67 0
016-
v^-»
6 2 c,
^V 3
•77V
7vsr
<^1 -*_
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Temp ,
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Room.
Temp.
V7
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5-7
6/
51
6/
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6-<;
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C. ?
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater^
Date Jl-'l-l
Sampling Location C/^e•>'/'{• cl
Sample Type <=j G-
Start Time
Stop Time
Run Number Q. -
Operator /fy
LO H
Ambient Temperature -
Barometric Pressure
Static Pressure, (P^Y
Filter Number(s) "
Meter \a p L/(e
Probe Length and type /// ••"£„
Pi tot Tube Coef ficient, •/ c/
Assumed Moi sture Wo
Sample Box Number_
<=>(,
Meter Box Number /(-"/V; - /\ ,
Meter II /-vj
7 (V
Pretest Leak Rate
Post Test Leak Rate,(i/T-
Read and Record All Data Every (; C Minutes
Clock Time
Sampling (24-hr
time.mln Clock)
O // o-O
1C, ,•=,
(& 3 O
u c *v^
IPO 11 |