United States
Environmental Protection
Agency
Office of Air Quality
PSanning and Standards
Research Triangle Park NC 27711
EMB Report
Nov1989
VOLUHE I
Air
EPA
Woodheater Test Method And
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 #
1.0
2.0
3.0
4.0
5.0
Appendix
A
B
C
D
E
F
H
I
J
K
Title Page
Introduction 1-1
Summary and Discussion of Results 2-1
Test Facilities and Methods 3-1
Wood Stove Specific Information 4-1
Appendices
VPI Method - Sampler Operation and Procedures A-l
Equipment QA/QC and Calibration B-l
VPI Gas Analysis Results C-l
Sample Blanks D-l
Graph Values and Formulas E-l
Proportionality Data and All Raw Run Data F-l
For Each AK-18 Test at Research Triangle Park
Proportionality Data and All Raw Run Data G-1
For Each CC-150 Test Conducted in ES Wood
Stove Lab
Proportionality Data and All Raw Run Data H-l
For The AK-18 Tests at Crested Butte
Proportionality Data and All Raw Run Data 1-1
For The AK-18 Tests at Crested Butte
Proportionality Data and All Raw Run Data J-1
For The S-173E Tests at Crested Butte
Proportionality Data and All Raw Run Data K-l
For The Ashley Oval Tests at Crested Butte
-------
LIST OF TABLES
Table # Description
2.1 Method 5G Compared to VPI Method ES 2-2
Laboratory RTF, NC
2.2 Sweet Home AK-18 RTF, NC Detailed 2-4
Method 5G and Calculated VPI Test Results
2.3 Country Comfort CC-150 RTF, NC Detailed 2-5
Method 5G and Calculated VPI Test Results
2.4 Sweet Home AK-18 RTP, NC VPI Test Results 2-6
2.5 Country Comfort CC-150 RTP, NC VPI Test Results 2-7
2.6 Carbon Monoxide Emissions for 2-8
Evaluation versus Burn Rate
2.7 Sweet Home AK-18 Crested Butte Results 2-10
2.8 Country Comfort CC-150 Crested Butte Results 2-11
2.9 Haugh's S-173E Crested Butte Results 2-12
2.10 Ashley Oval Crested Butte Results 2-13
2.11 VPI Results Crested Butte 2-14
2.12 Test Specific Method Deviations 2-22
and Resolutions
3.1 Crested Butte Test Program Overview 3-19
4.1 Modified Sweet Home AK-18 Description 4-3
4.2 Description of AK-18 Before Modifications 4-4
n
-------
LIST OF FIGURES
Figure # Description Page
1.1 Actual VPI versus Actual Method 5G 1-4
Emission Rates For All Tests
1.2 VPI Carbon Monoxide Comparison For Sweet 1-5
Home AK-18 and Country Comfort CC-150
2.1 Actual VPI versus Actual Method 5G 2-3
Emission Rates For All Tests
2.2 VPI Carbon Monoxide Comparison For Sweet 2-9
Home AK-18 and Country Comfort CC-150
2.3 Emission Results For Sweet Home AK-18 at 2-16
Different Elevations While Burning Douglas
Fir Cribs
2.4 Emission Rates For Country Comfort CC-150 2-17
at Different Elevations While Burning
Douglas Fir Cribs
2.5 Emission Rates Sweet Home AK-18 Normal 2-18
Burning of Cordwood versus Modified Method 28
2.6 Emission Rates Country Comfort CC-150 2-19
Normal Burning of Cordwood versus Modified
Method 28
2.7 Emission Rates Haugh's S-173E Normal Burning 2-20
of Cordwood versus Method 28 at 300 Feet
2.8 Emission Rates/Ashley Oval Emission Rates 2-21
For Normal Cordwood Burning
3.1 RTP Wood Stove Test Facility As Used For 3-2
VPI Test Series Top View
3.2 RTP Wood Stove Test Facility As Used For 3-3
VPI Test Series Side View
3.3 Mt. Mitchell Test Facility Used For Elevation 3-4
Testing-1988 Top View
3.4 Mt. Mitchell Test Facility Used For Elevation 3-5
Testing-1988 Side View
3.5 Overview of The Crested Butte Stove Test 3-6
Facility
23.40
A.LOT iii
-------
LIST OF FIGURES
(CONTINUED)
Figure # Description Page
3.6 Test Configuration for Individual Stove At 3-7
Crested Butte
3.7 Engineering-Science Method 5G Sampling Train 3-9
3.8 Engineering-Science Method 5G Filter Holder/ 3-10
Probe Assembly
3.9 Method 5G For Sweet Home AK-18 RTP Facility 3-11
Vertical Duct-Dual Train
3.10 Method 5G For Country Comfort CC-150 RTP 3-12
Facility Horizontal Duct-Dual Train
3.11 VPI Sample Train Configuration For Comparison 3-13
Testing
3.12 Schematic of VPI In Home Sampler 3-14
3.13 Data Sheet Used For VPI In-Situ Testing 3-15
3.14 Method 5G Sampling Train Configuration As 3-16
Used At Crested Butte
4.1 Modified Sweet Home AK-18 Showing Gas Flows 4-2
4.2 Schematic of Original and Modified CC-150 4-5
Detailing Modifications
4.3 Modified CC-150 Representative Gas Flows 4-6
4.4 Haugh's S-173E With Representative Gas Flows 4-8
123.40
1A.LOT
IV
-------
SECTION 1.0
-------
SECTION 1.0
INTRODUCTION
Engineering-Science (ES) was directed by the U.S. Environmental Protection
Agency (EPA), Emissions Measurement Branch (EMB) (Subcontract No. 2-89-
0055) to conduct testing to determine the relationship of results, if any, between the
Virginia Polytech Institute and State University (VPI) sampling method and EPA
Methods 5G/28. A secondary part of the testing program was conducted at Crested
Butte, Colorado elevation -8900 feet. The effects of elevation on both particulate
and Carbon Monoxide (CO) emissions, the emissions of regular cordwood versus
Method 28 test fuel, and the emission of a low tech (Ashley Oval) stove were to be
examined in conjunction with the VPI versus EPA Method 5G study.
TEST PROGRAM RESEARCH TRIANGLE PARK NORTH CAROLINA
The first series of tests were conducted at the ES Wood Stove Laboratory in
Research Triangle Park, NC (elevation -300 feet), between September 21 and
October 10, 1989. This test series consisted of eight test days for the Modified
Sweet Home AK-18, S.N. 0662 and eight test days for the Modified Country
Comfort CC-150, S.N. 750-4865CC. (These wood stoves are the same stoves used
for the 1988 and 1989 laboratory accreditation test as well as the elevation testing at
Mt. Mitchell, NC in the fall of 1988). Each test day was approximately 10 hours in
length. Each test included (2) EPA Method 5G trains and (2) VPI trains; all four
trains were run simultaneously. The tests were started after a pre-burn and followed
EPA Method 28 with two major exceptions. The exceptions being:
1. When the fuel crib had burned to zero weight a new fuel crib (or partial
fuel crib) was added so that the stove could burn at the desired rate for
approximately 10 hours.
2. If it was determined that the final fuel crib would not be consumed within
11-12 total test hours, the primary air was fully opened to speed the process.
TEST PROGRAM CRESTED BUTTE. COLORADO
The test program conducted at Crested Butte, elevation -8900 feet, consisted
of three 70 hour test series using four wood stoves. The wood stoves used were:
• Sweet Home AK-18 S.N. 0662
• Country Comfort CC-150 S.N. 750-4865 CC
• Haughs S-173E S.N. 792570
• Ashley Oval (provided on site) S.N. (unknown)
123.40
1ARPT 1-1
-------
The cordwood testing at Crested Butte was done by the following protocol:
• The test day started when the sample trains were turned on.
• Cold start (first day of each six day test series) the sampling trains were
started just prior to starting the fire.
• Hot start (remaining day of each test series) the woodstoves werekept
burning through the night to retain heat in the woodstove after each
test day, to insure us ofa hot start The trains were started just prior to
loading the stove with the first day charge.
• The test day ended when the desired length of the test day had passed.
• The fuel weight at the end of the test day was always approximately the
same as the weight at the start of the day (before any wood was added).
• Logs were placed in the stove after testing to keep the stove hot
through the night.
» Four wood stoves were tested during the first two test series by the method
above.
• For the third test series Haughes and Ashley were tested as outlined above.
The Country Comfort and the Sweet Home AK-18 were tested for four days
each, during the third test series, using the same Modified EPA 28 described as
being used in the ES's RTF facility.
Engineering-Science has done many wood stove test using dual Method 5G
sampling trains. The emission rates from each train are typically within 10% of each
other.
The 16 dual VPI tests that were done at ES's RTF facility showed the VPI
emission rates for each train to be comparable. The dual train 5G and VPI results
are shown in Tables 22 and 23 of this report. Based on the RTF results it was
concluded that one Method 5G and one VPI could be used for each stove. The
Method 5G and VPI sampling trains were run simultaneously.
The Sample Trains were recovered daily during the Modified Method 28
Testing. During the 70 hour cordwood tests, the Method 5G filters were recovered
daily. However, the probe and front filter bell were not recovered until the end of
the 70 hour test series.
The VPI samplers were set at a 8 milliliters per minute flow rate for the 70 hour
cordwood tests, and at 60 miHuiters per minute for the Modified EPA Method 28
Tests.
113.40
1A.RPT 1-2
-------
TEST RESULTS
The basic findings of the study are:
VPI Versus EPA Method 5G Results
The results of the VPI versus Method 5G are presented in Figure 1-1. The VPI
Train always gives a higher emission rate than Method 5G using the actual
calculated emission rates, before corrections, for each train.
However, the VPI emission rate can be corrected to Method 5G and 5G
adjusted emission rates with good correlation. The equations for converting VPI
results to 5G or 5G adjusted to 5H are given below.
For VPI to 5G:
5G = (0.712)(VPI ACTUAL)-.261
The Limits of Prediction of Y for a given X
(LPY for X) = 1.47
R Squared = 0.973
Number of Observations = 50
For VPI to 5G (Adjusted):
5G(Adj) = (0.728(VPI Actual)+1.095
LPY for X = 1.48
R Squared = 0.974
Number of Observations = 50
Effect of Elevation on Carbon Monoxide Emission Rates
The Carbon Monoxide (CO) results are calculated in gm/hr by the VPI
Sampler program. Elevation does not seem to make a significant difference as long
as the burn rates are equal see Figure 1.2. However, it is not possible to achieve
burn rates with the two woodstoves that were tested at the two higher elevations.
Effect of Elevation on Particulte Emission Rates
The AK-18 and CC-150 were tested using a modified Method 28, in the ES
Woodstove Lab and at Created Butte. The same stoves were tested at Mt. Mitchell,
NC using Method 28. The lab elevation is -300 feet. Mt. Mitchell was -5800 feet
and Crested Butte was -8900 feet
•123.40
1ARPT 1-3
-------
WOODSTOVE LAB AND CRESTED BUTTE
3
O
I
l/l
2
or
e>
o
1O
Q
O
I
20 -
15 -
10 -
5 -
ALL TESTS VPI vs 5G ACTUAL
VPI(ACT) COHVJUSIOK TO 5GCACT)
USED OX ALL VPI SUHS
Regression Output:
Constant
Sid Err of T Est
t Squired
Xo. of Observations
Decrees of frtedcn
X Coefficients)
std Err of Cat I.
5C-<-712HV?l Aa)-.21o
VPI ACTUAL GRAMS HOUR
0 VPI(ACT) vs 5G(ACT)
VPI BEST FIT
Figure 1.1 Actual VPI Versus Actual Method 5G Emission Rates for All Tests
1-4
-------
VPI CO RESULTS AK-18 AND CC150
a b
LAS vs CRESTED 8UTTE
x
33
U
U
o
X
o
o
2
2
O
03
5
o
220
210
200
190
180
170
160
150
140
130
120
110
100
90
80
70
60
50
40
30
20
10
0
-f-
+
0.4 0.6 0.8
1
1.2 1.4 1.6 1.8
_ BURN RATE KG/HR
D LAS AK-18 + LAB CC 150 o CRESTED 8UTTE AK-18 A CRESTED 8UTTE CC150
a. outliers S-3A and 3B not used
b. results of cordwood tests not used
Figure 1.2 VPI Carbon Monoxide Comparison for Sweet Home AK-18 and Country
Comfort CC-150
1-5
-------
The results show the emission rate is related to the burn rate. While a higher
elevation decreases the maximum burn rate, higher elevation does not significantly
change the emission rate for a given burn rate.
Use of Cordwood Versus Method 28 Test Fuel
The cordwood was to be representative of typical wood burned in Crested
Butte. The cordwood burned during the tests was a mixture of spruce and pine
which were taken from the forest as standing deadwood. The standing deadwood
had approximately 8-12% moisture on a dry basis. During the second and third test
series the standing deadwood was mixed with fresh cut Douglas fir of approximately
30-55% moisture on a dry basis. The cordwood supplier indicated that this mixture
was normal firewood for Crested Butte.
The daily values for the cordwood tests include only the filter weight gain and
are therefore somewhat lower than actual (<5%). In addition, it can be seen that
cordwood and normal operating practices seem to adversely affect the AK-18
emissions. The AK-18 averaged 102 gm/hr with cordwood versus 2.3 gm/hr using
Modified Method 28. The CC-150 averaged 2L3 gm/hr with cordwood and 19.7
gm/hr with Modified Method 28. The S-173-E averaged 13.9 grn/hr with cordwood.
The S-173E averaged 13.2 gm/hr during its baseline testing at 300 feet elevation,
during the 1990 laboratory accrediation program, using Methods 5G/28. The
Ashley average 29.3 gm/hr with cordwood. The Ashley was only tested while
burning cordwood at Crested Butte. The above values are based on Method 5G
adjusted values to 5H equivalent.
This report is organized as follows:
• Section 1 Introduction
• Section 2 Summary and Discussion of Results
• Section 3 Test Facilities and Methods
• Section 4 Wood Heater Specific Information
a Section 5 Includes all Appendices
Appendix A VPI Method Sampler Operational and
Procedures.
Appendix B Equipment QA/QC and Calibration
Appendix C VPI Gas Analysis Results
Appendix D Sample Blanks
Appendix E Graph Values and Formulas
Appendix F Proportionality Data and All Raw Run Data for
Each AK-18 Test Conducted in ES Woodstove
Lab
) 123.40
51A.RPT 1-6
-------
Appendix G
Appendix H
Appendix I
Appendix J
Appendix K
Proportionality Data and All Raw Run Data for
Each CC-150 Test Conducted in ES Woodstove
Lab
Proportionality Data and All Raw Run Data for
the CC-150 Tests at Crested Butte
Proportionality Data and All Raw Run Data for
the AK-18 Tests at Crested Butte
Proportionality Data and All Raw Run Data for
the S-173E Tests at Crested Butte
Proportionality Data and All Raw Run Data for
the Ashley Oval Tests at Crested Butte
Due to the large volume of data generated this report is divided into 2
volumes. Volume 1 contains Section 1,2,3 and 4 plus Section 5 Appendices A, B, C,
D, E, F and G. Volume 2 contains Section 5 Appendices H, I, J and K
D123.40
151A.RPT
1-7
-------
SECTION 2.0
-------
SECTION 2.0
SUMMARY AND DISCUSSION OF RESULTS
The Test Program consisted of two parts. The first part was conducted at the
Engineering-Science Woodstove Test Facility in Research Triangle Park, North
Carolina, which is at approximately 300 feet elevation. The objective was to
determine if the VPI Test Method, as used in the 1988-1989 Crested Butte,
Colorado study, was comparable to the USEPA Methods 28/5G presently being
used for woodstove certification and laboratory accreditation.
The previously tested woodstoves Sweet Home AK-18 Serial# 0662 and the
Country Comfort CC-150 Serial# 790-4865CC were tested at R.T.P. for a total of
eight test runs each. The burn rates were varied in an attempt to have two test runs
at each of the four burn rates. However; the highest burn rate achieved for either
stove was 1.88 (kg/hr) kilogram per hour compared to 132 (kg/hr) at Crested
Butte. The results of this first test series are presented in Table 2.1. It will be
noticed that the VPI method always produced an actual emission rate which was
higher than the actual Method 5G (NOT ADJUSTED TO 5H EQUIVALENT)
emission rate.
Based on the good correlation found between the Method 5G and VPI tests as
shown in Figure 2.1. It was decided too proceed to Crested Butte, Colorado for the
second part of this test program,
A more detailed report of the test results can be seen in Tables 2.2,2.3,2.4 and
2.5. Table 2.2 shows the detailed results of the Method 5G testing with calculated
emission rates of the VPI samplers for each test of the Sweet Home AK-18. Table
2.4 shows the results for each VPI test of the AK-18 done in ES's RTF laboratory
facility. Tables 2.3 and 2.5 likewise show a detailed breakdown of results for each
RTF test run of the Country Comfort CC-150.
The second part of the test program was the determination of elevation effects
on the amount of carbon monoxide and particulate emitted by a woodstove. Also
the comparison of data on burning cordwood versus crib wood.
The average carbon monoxide value for each VPI test run was determined by
analyzing the tanks gases. The results of these tests are shown in Table 2.6. Figure
22 shows the results in graphic form. It can be seen that the effect of elevation
seems to be fairly small when the burn rate is taken into account. Due to the
limited number of tests and burn rates at Crested Butte the graph is mainly of value
as visual aid.
The results of the Crested Butte portion of the test program are presented in
Tables 2.7 through 2.11. Table 2.7 presents detailed Method 5G results with
calculated VPI results for the Sweet Home AK-18. Table 2.8 shows results for the
Country Comfort CC-150, Table 2.9 shows results for the Haughes S-173 and Table
2.10 is results for the Ashley Oval. Table 2.11 presents the details of all the VPI
tests at Crested Butte.
23.40
A.RPT 2-1
-------
TABLE 2.1
METHOD 5G COMPARED TO VPI METHOD
ES LABORATORY RTF, NC
Run#
Sweet Home
SH-3
SH-2
SH-8
SH-7
SH-6
SH-1
SH-4
SH-5
Burn Rate
kg/hr
0.61
0.74
1.04
1.14
1.33
1.56
1.81
1.88
5G Actual'
Emission Rate
grn/hr
13.73
0.60
0.87
1.14
1.28
1.44
1.95
1.38
VPI Corrected1
Emission Rate
gm/hr
11.31
0.45
0.98
1.02
1.52
2.02
1.57
1.24
VPI Actual15
Emission Rate
gm/hr
16.2
1.0
1.7
1.8
2.5
3.2
2.6
2.1
Country Comfort
CC5-6 0.45
CC5-5 0.78
CC5-7 0.82
CC5-1 1.17
CC5-3 1.39
CC5-4 1.49
CC5-8 1.68
CC5-2 1.86
15.83
22.76
15.45
14.85
13.84
8.78
5.51
7.49
14.62
21.10
16.64
16.04
13.23
8.89
4.51
6.26
The formula used to correct the VPI Emission Rate is:
20.9
30.0
23.8
22.8
19.0
12.8
6.7
9.2
CORRECTED VPI = (0.712)(ACTUAL VPI) - 0.261
This formula was derived from both the ES lab and Crested Butte Tests
"Average of two sampling trains
123.40
1A.RPT
2-2
-------
WOODSTOVE LAB AND CRESTED BUTTE
40
35
30
25
20
15
10
ALL TESTS VPI vs 5G ACTUAL
a:
o
o
o
HI
Q
O
t
2
VJ>I(ACT) CONTOtSIOH TO 5G
-------
METHOD 5C EMISSION RATE CALCULATIONS
ts>
Jtv manui tWEET HOME
Hod«l Hoi AK-18
Lob nanwt IS WOOOSTOVE LAD RIP
T«t Dttti SEPT-OCT,1989
tun Ho.l
Pb(__Hg)i
Tm(avg)i
dH(ivg)t
OCH, Y 1
DGMl i
DGHf t
ms(frnt)i
mg(fl*1)t
ma(n«)I
Qi(ivg) t
ER(9/hr)l
Eft(HSH) 1
BR(kg/hr)i
SH-1A
29.74
100.0
0.609
1.007
0.000
242.924
1.40
31.20
4.50
145.77
1.42
2.44
1.54
JK-1B
29.74
107.4
0.950
1.024
344.202
MO. 942
1.10
38.10
4.40
145.77
1.44
2.49
1.54
SH-2A
30. U
69.3
0.600
1.007
290.402
599.547
5.70
14.10
-0.10
150.52
0.59
1.17
0.74
Calculation Information
1-iMtrlc,2"Englthi 2.000
Oi, 1"/mln,2«/hr I 1.000
Lib iltltudt (ft)i 300.000
SH-2B
30.12
92.3
0.900
1.024
441. 738
947.980
4. '40
15.40
0.00
150.52
0.40
1.19
0.74
SH-3A
29.57
91.1
o.soo
1.007
603.303
910.045
6.80
425. 40
5.50
150.77
13.53
15.81
0.41
SH-3B
29.57
94.4
0.950
1.024
948.503
1252.412
8.60
437.40
4.40
150.77
13.93
14.20
0.41
SH-4A
29.74
99.5
0.800
1.007
53.063
325.132
4.30
47.30
3.90
146.92
1.97
3.19
1.81
SH-41
29.74
99.4
0.950
1.024
253.028
524.417
10.20
45.50
1.50
146.92
1.93
3.14
1.81
SH-5A
29.81
90.8
0.800
1.007
324.105
636.605
6.40
36.20
4.00
147.94
1.38
2.38
1.68
S 11-58
29.81
94.0
0.950
1.024
525.800
834.959
4.20
38.10
4.90
147.94
1.39
2.39
1.88
SH-6A
29.82
90.4
O.BOO
1.007
434.402
927.423
4.40
34.30
3.80
145.24
1.32
2.29
1.33
SH-6B
29.82
93.9
0.950
1.024
836.404
1126.118
7.70
32.00
0.40
145.26
1.24
2.17
1.33
SH-7A
29.46
98.0
0.800
1.007
930.003
1224.215
4.50
29.90
4.10
137.01
1.14
2.02
1.14
IH-7B
29.64
99.0
0.950
1.024
130.002
423.811
4.60
29.70
4.50
137.01
1.13
2.01
1.14
SH-BA
29.94
86.3
0.800
1.007
225.000
499.735
3.30
18.50
2.60
144.59
0.79
1.50
1.04
SH-flB
29.94
88.8
0.950
1.024
425.001
699.714
8.90
16.20
4.60
144.59
0.95
1.74
1.04
VTI ACIi 3.100 3.300 1.000 1.000 16.400 16.100 2.900 2.200 1.600 2.600 2.300 2.700 1.900 1.700 1.700 1.800
VP1 by VPI 2.900 3.100 1.100 1.100 12.300 12.100 2.800 2.200 1.700 2.500 2.300 2.600 1.900 1.800 1.800 1.800
TO 5Q (s/hr)
VPI by ESt 1.944 2.089 0.451 0.451 11.414 11.202 1.804 1.305 0.878 1.590 1.377 1.661 1.092 0.949 0.949 1.021
TO 5G (g/hr)
VPI by ESI 3.352 3.497 1.623 1.823 13.034 12.816 3.206 2.697 2.260 2.988 2.769 3.041 2.478 2.333 2.333 2.405
TO 5H (g/hr)
VPI CO: 20.900 34.100 27.600 26.200 198.900 199.900 80.900 79.100 52.100 51.500 21.400 22.500 13.400 13.200 8.100 8.900
Run Ho.l 5H-1A SH-U SH-2A SH-2B SII-3A SH-3B SH-4A SH-4B SH-5A SH-5B SH-6A SH-6B SK-7A SH-7B SH-BA SH-8B
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METHOD 5G EMISSION RATE CALCULATIONS
Stv iMnuiCOUHTRY COMFORT Calculation Information
Model HoiCC-150 1-metrlc,2
a,
-------
SUN «
SH-1A
SH-18
SH-2A
SH-2B
SH-3A *
SH-3B •
SH-4A
SH-4B
SH-5A
SH-58
SH-4A **
SH-6B
SH-7A
SH-7B
SH-8A
SH-88
RUN t
SH-1A
SH-1B
SH-2A
SH-2B
SH-lA
SH-38
SH-'A
iH-48
SH-5A
SH-58
SH-6A
3H-6B
SH-7A
SH-7B
SH-8A
SH-33
RUN »
SH-1A
SH-1B
SH-2A
SH-2B
SH-3A
SH-3B
SH-4A
SH-4B
SH-5A
SH-S8
SH-4A
SH-6B
SH-7A
SH-7B
SH-SA
SH-88
RUN *
SH-1A
SH-1B
SH-2A
SH-2B
SH-3A
SH-3B
SH-4A
SH-4B
SH-5A
SK-5B
SH-6A
SH-68
SH-7A
SH-7B
SH-8A
SH-88
Tank
C02
Z
12.34
12. 34
14.44
14.74
8. 74
3.64
14.24
14.04
- 14.24
14.40
14.64
14.64
15.22
15.40
15.27
15.27
Frruir
rant
Filter
g pre
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
SH-1A
SH-1B
SH-2A
SH-2B
SH-3A
SH-3B
SH-4A
SH-48
SH-5A
SH-5B
SH-6A
5H-6B
SH-7A
SH-7B
SH-8A
SH-88
UOQO DATE
RUN * HEATER RETRIEVED
MODEL
SH-1A AK-18 09-21-89
SH-1B AK-18 09-21-89
SH-2A AK-18 09-28-89
SH-2B AK-18 09-28-89
SH-3A AK-18 10-02-89
SH-38 AK-18 10-02-89
SH-4A AK-18 10-03-89
SH-48 AK-18 10-03-89
SH-5A AK-18 10-04-89
SH-5B AK-18 10-04-89
SH-6A AK-18 10-05-89
SH-68 AK-18 10-05-89
SH-7A AK-18 10-06-89
SH-78 AK-18 10-06-89
SH-8A AK-18 10-09-89
SH-88 AK-18 10-09-89
Tank
CO
X
0.20
0.23
0.47
0.45
3.93
3.91
0.56
0.54
0.34
0.34
0.20
0.21
0.15
0.15
0.10
0.11
Filter
9 post
-0.0006
0.0005
0.0019
-0.0001
0-0540
0.0503
0.0019
0.0009
0.0021
0.0016
0.0008
-0.0006
0.0016
0.0013
0.0004
0.0005
Gas
MU
g/mol
30.3
30.3
30.6
30.7
30.4
30.3
30.6
30.6
30.6
30.6
30.6
30.6
30.7
30.7
30.7
30.7
Tank
02
X
7.37
a. oo
5.62
5.24
10.00
10.00
5.99
6.24
6.19
5.99
5.69
5.74
5.12
4.99
4.99
5.02
Filter
g pre
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Air/
Fuel
9.3
9.8
8.2
8.1
8.5
8.5
8.2
3.3
8.4
8.3
8.3
8.3
8.0
7.9
8.1
8.1
--
TOTAL
CATCH
3
0.0076
0.0082
0.0077
0. 0071
0.1330
0.1264
0. 0074
0.0055
0.0047
0.0073
0.0085
0.0103
0.0089
0.0076
0.0083
0.0089
Filter
g post
0.0004
-0.0008
-0.0002
-0.0011
0.0008
0.0000
0.0002
-0.0008
0.0005
-0.0008
0.0004
-0.0003
-0.0004
-0.0010
-0.0003
-0.0005
SAMFLO
dry g/s
0.00120
0.00119
0.00136
0.00127
0.00122
0.00120
0.00124
0.00125
0.00130
0.00125
0.00126
0.00129
0.00127
0.00124
0.00129
0.00130
FUEL
TYPE
O.FIR
D.FIR
D.FIR
D.FIR
D.FIR
O.FIR
O.F:R
D.FIR
D.FIR
O.FIR
D.FIR
O.FIR
O.FIR
O.FIR
O.FIR
O.FIR
LOADED
FUEL
wet kg
17.69
17.69
9.30
9.30
7.57
7.57
19.91
19.91
23.63
23.63
15.78
15.78
13.79
13.79
11.75
11.75
FUEL MC
dry X
*3CTSS
22.90
22.90
22.40
22.40
22.70
22.70
22.40
22.40
22.40
22.40
23.30
23.30
23.30
23.30
23.20
23.20
=J3'J-K3333
EOUIV
COAL BURNED
BED FUEL
kg uet kg
0.00 17.49
0.00 17.69
0.00 9.30
0.00 9.30
0.00 7.37
0.00 7.57
0.00 19.91
0.00 19.91
0.00 23.43
0.00 23.63
0.00 15.78
0.00 15.78
0.00 13.79
0.00 13.79
0.00 11.75
0.00 11.75
INITIAL FINAL TOTAL EOUIV FINAL
HOUR HOUR SAMPLING BURN TANK
METER METER TIME RATE TEMP
hr hr hr dry kg/hr c
0.00 9.22 9.22 1.56 21.00
0.00 9.22 9.22 1.56 21.00
0.00 10.25 10.25 0.74 21.00
0.00 10.25 10.25 0.74 21.00
0.00 10.08 10.03 0.61 20.00-
0.00 10.08 10.08 0.61 20.00
0.00 9.00 9.00 1.81 20.50
0.00 9.00 9.00 1.81 20.50
0.00 10.28 10.28 1.88 21 00
0.00 10.28 10.28 1.88 21.00
0.00 9.63 9.63 1.33 21.00
0.00 9.63 9.63 1.33 21.00
0.00 9.80 9.30 1.14 20.00
0.00 9.80 9.30 1.14 20.00
0.00 9.17 9.17 1.04 22.00
0.00 9.17 9.17 1.04 22.00
3==a===========a=3S3=ss=53=3s==
PROBE PROBE LINE LINE
PM
g/hr
3.1
3.3
1.0
1.0
16.4
16.1
2.9
2.2
1.6
2.6
2.3
2.7
1.9
1.7
1.7
1.3
Tare we.
9
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
K2
dry X
79.69
79.55
79.71
79.80
79.30
79.41
79.49
79.45
79.40
79.44
79.57
79.52
79.59
79.54
79.69
79.66
CO
g/hr
29.8
34.1
27.8
26.2
198.9
199.9
80.9
79.1
52.1
51.5
21.4
22.5
13.4
13.2
8.1
5.9
(w/rej.J
g
0.0070
0.0063
0.0081
0.0078
0.0719
0.0707
0.0069
0.0084
0.0057
0.0067
0.0071
0.0108
0.0068
0.0096
0.0056
0.0065
RHO
kg/n~3
0.54
0.53
0.68
0.64
0.60
0.59
0.55
0.55
0.65
0.63
0.60
0.61
0.61
0.59
0.58
0.58
CO
g/kg
19.1
21.3
37.5
35.3
324.9
326.6
'4.7
43.8
27.7
27.4
16.1
16.9
11.7
11.4
7.3
3.6
Tant
i ante
Pressure
tor pre
4.30
3.00
2.50
2.50
3.00
3.00
2.50
2.50
2.30
2.30
2.30
2.30
2.50
2.50
1.80
1.80
STWLOU
dry 3/3
4.49
4.44
1.80
1.77
1.52
1.54
4.39
4.45
4.65
4.60
3.24
3.25
2.71
2.43
2.48
2.47
PH
9AS
1.98
2.15
1.34
1.30
26.36
26.29
1.61
1.20
0.37
1.40
1.71
2.03
1.69
1.47
1.66
1.77
Tant
lame
Pressure
tor post
~~ _
331.00
326.00
410.00
384.00
366.00
359.00
329.00
332.00
394.00
378.00
359.00
365.00
366.00
355.00
350.00
352.00
. j -:«^±=3
pre wt. post we. pre uc. post uc.
SH-U
SH-1B
SH-2A
SH-2S
SH-3A
SH-38
SH-4A
SH-4B
SH-5A
SH-5B
SH-6A
SH-68
SH-7A
SH-7B
SH-SA
SH-88
g
0.0000 0
0.0000 0
0.0000 -0
0.0000 0
0.0000 0
0.0000 0
999
.0010 0.0000 -0.0002
.0018 0.0000 0.0004
.0021 0.0000 0.0000
.0005 0.0000 0.0000
.0054 0.0000 0.0009
.0039 0.0000 0.0010
0.0000 -0.0011 0.0000 -0.0005
0.0000 -0
.0028 0.0000 -0.0002
0.0000 -0.0028 0.0000 -0.0008
0.0000 -0
0.0000 0
.0002 0.0000 0.0000
.0006 0.0000 -0.0004
0.0000 0.0004 0.0000 0.0000
0.0000 0.0012 0.0000 -0.0003
0.0000 -0.0016 0.0000 -0.0007
0.0000 0.0011 0.0000 0.0015
0.0000 0.0009 0.0000 0.0015
PROBE LINE
0.
0.
-0.
0.
0.
0.
9 9
0010 -0.0002
ooia 0.0004
0021 0.0000
0005 0.0000
0054 0.0009
0039 0.0010
-0.0011 -0.0005
-0.
-0.
-0.
0.
0.
0.
-0.
0.
0.
0028 -0.0002
0028 -0.0008
0002 0.0000
0006 -0.0004
0004 0.0000
0012 -0.0003
0016- -0.0007
0011 0.0015
0009 0.0015
FILTER FILTER Residue
999
-0.0006 0.0004 0.0070
0.0005 -0.0008 0.0063
0.0019 -0.0002 0.0081
-0.0001 -0.0011 0.0078
0.0540 0.0008 0.0719
0.0508 0.0000 0.0707
0.0019 0.0002 0.0069
0.0009 -0.0008 0.0034
0.0021 0.0005 0.0057
0.0014 -0.0008 0.0067
0.0008 0.0004 0.0071
-0.0006 -0.0003 0.0108
0.0016 -0.0004 0.0068
0.0013 -0.0010 0.0096
0.0004 -0.0003 0.0056
0.0005 -0.0005 0.0065
Table 2.4 Sweet Home AK-18 RTF, NC VPI Test Results
2-6
-------
J UJ
3
i UJ
RUN *
CC5-1A
ccs- la
CC5-2A
CCS -28
CC5-3A
CCS -38
CC5-4A
CC5-48
CCS-5A
CC5-58
CCS-6A
CCS-6B
CC5-7A
CC5-7B
CC5-8A
CCS -88
RUN *
CC5-U
CC5-18
CC5-2A
CC5-2B
CCS-3A
CCS-38
CC5-4A
CC5-4B
CCS-5A
CCS-58
CCS -6*
CC5-68
CC5-7A
CCS -78
CC5-8A
WOOD DATE
RUN # HEATER RETRIEVED
HOOEL
* CC5-1A CC150 09-21-89
CC5-1B CC150 09-21-89
CCS-2A CC150 09-25-89
CCS-2B CC1SO 09-2S-89
•* CC5-3A CC150 09-26-89
CC5-3B CC150 09-26-89
CC5-4A CC1SO 09-27-89
CCS-43 CC150 09-27-89
CC5-5A CC150 09-28-89
CCS-5B CC150 09-28-89
CC5-6A CC1SO 10-02-89
CC5-6B CC150 10-02-89
CC5-7A CC150 10-09-89
CC5-7B CC150 10-19-89
CC5-8A CC150 10-10-89
CC5-8B CC150 10-10-89
Tank
C02
X
5.25
7.15
8.94
8.94
8.94
8.74
9.34
9.24
7.65
7.65
5.05
5.05
7.04
6.95
9.14
CCS-88 9.14
RUN g
CC5-1A
CCS- 18
CCS-2A
CCS-28
CC5-3A
CC5-3B
CCS-4A
CCS-48
CCS-SA
CCS-58
CC5-6A
CCS -68
CC5-7A
CC5-7B
CCS-8A
CCS-88
RUN «
CCS- U
CC5-1B
CC5-2A
CC5-2S
CC5-3A
CC5-38
CCS-4A
CCS-4B
CCS-SA
CC5-5B
CCS-6A
CCS-68
CCS-7A
CCS-78
CCS-8A
CCS-88
Front
Filter
3 pre
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
o.oooo
0.0000
o.oooo
o.oooo
o.oooo
0.0000
0.0000
CCS-1A
CCS-1B
CC5-2A
CCS -28
CC5-3A
CCS-3B
CCS-4A
CC5-4B
CCS-5A
CC5-5B
CCS-6A
CCS-6B
CC5-7A
CC5-7B
CCS-SA
CCS-88
Tank
CO
X
0.92
1.28
0.67
0.64
1.21
1.18
1.04
1.01
1.81
1.83
2.71
2.71
1.87
1.87
0.34
0.33
Front
Filter
9 f»st
0.0176
0.0234
0.0061
0.0064
0.0141
0.0169
0.0122
0.0098
0.0479
0.0494
0.0527
0.0497
0.0245
0.0394
0.0062
0.0060
Gas
mi
g/mol
29.6
29.9
30.0
30.0
30.1
30.0
30.1
30.1
30.0
30.0
29.8
29.8
29.9
29.9
30.0
30.0
Tank
02
X
15.25
13.13
11.50
11.38
11.00
11.13
10.88
11.13
11.75
11.75
14.38
14.46
12.75
12.95
11.08
11.20
Back
Filter
9 pre
0.0000
0.0000
o.oooo
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
Air/
Fuel
18.6
13.6
12.4
12.5
11.5
11.8
11.3
11. S
12.0
12.0
13.6
13.5
12.6
12.7
11.9
11.9
TOTAL
CATCH
3 (A)
0.0493
0.0607
0.0142
0.0136
0.0339 '
0.0435
0.0308
0.0258
0.1199
0.1268
0.1254
0.1201
0.0904
0.0904
0.0125
0.0127
Back
Filter
g post
0.0000
-0.0004
-0.0004
-0.0010
-0.0001
-0.0007
0.0002
-0.0007
-0.0012
0.0001
0.0011
-0.0002
0.0098
0.0002
-0.0001
-0.0005
SAMFLO
dry g/s
0.00141
0.00124
0.00123
0.00125
0.00106
0.00122
0.00139
0.00126
0.00125
0.00125
0.00120
0.00118
0.00124
0.00120
0.00124
0.00124
FUEL
TYPE
D.F1R
O.FIR
O.FIR
D.F1R
O.FIR
O.FIR
O.fIR
O.FIR
O.FIR
O.FIR
O.FIR
O.FIR
D.FIR
O.FIR
O.FIR
O.FIR
PH
g/hr
22.5
23.3
9.4
8.9
17.7
20.2
13.3
12.4
29.3
30.7
21.2
20.6
23.3
24.2
6.6
6.3
Beaker
Tare wt.
g
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
o.oooo
o.oooo
0.0000
N2
dry X
79.04
79.08
79.23
79.36
79.46
79.54
79.26
79.13
79.70
79.69
79.22
79.14
79.28
79.17
79.36
79.25
LOADED
FUEL
wet kg
13.65
13.65
18.55
18.55
14.15
14.15
14.79
14.79
8.39
8.39
4.85
4.85
9.34
9.34
17.83
17.83
CO
9/hr
194.2
197.7
1S0.6
144.3
188.4
188.2
170.4
167.4
163.9
165.2
163.0
162.9
187.S
189.0
163.1
161.1
Beaker
(w/res.J
9
0.0272
0.0354
0.0077
0.0084
0.0180
0.0264
0.0156
0.0161
0.0707
0.0744
0.0736
0.0679
0.0555
0.0490
0.0087
0.0086
RHO
kg/m-3
0.66
O.SS
0.49
0.50
0.43
0.50
0.56
o.so
0.54
0.54
0.51
0.51
0.56
0.55
0.53
0.53
xavxwmxtxa
FUEL MC
dry X
21.60
21.60
22.00
22.00
21.30
21.30
21.90
21.90
22.60
22.60
21.50
21.50
22.20
22.20
20.30
20.80
CO
9/ks
166.4
169.5
80.9
77.3
135.7
135.5
114.8
112.3
211.5
213.2
358.6
358.3
228.9
230.7
97.2
96.1
Tank
Pressure
tor pre
3.00
4.30
2.30
2.30
3.30
3.30
5.10
3.80
2.50
2.SO
3.00
3.00
1.80
4.30
2.30
2.30
STKFLOU
dry g/i
6.19
4.57
6.69
6.73
4.64
4.7S
4.89
4.9S
2.69
2.68
1.78
1.78
2.98
3.00
5.78
S.78
EOUIV INITIAL FINAL IQIAL ECUIV FINAL
COAL BURNED HCUR HOUR SAMPLING BURN TANK
BED FUEL METER HETER TIME RATE TEMP
kg net kg hr hr hr dry kg/hr C
0.00 13.65 Q.OO 9.62 9.62 1.17 21.00
0.00 13.65 d.OO 9.62 9.62 1.17 21.00
0.00 18.55 0.00 8.17 8.17 1.86 21.00
0.00 18.55 0.00 8.17 3.17 1.S6 21.00
"0.00 14.15 0.00 8.40 3.40 1.39 20.50
0.00 14.15 0.00 8.40 8.40 1.39 20.50
0.00 14.79 0.00 8.17 8.17 1.49 22.00"
0.00 14.79 0.00 8.17 8. 17 1.49 22.00
0.00 3.39 0.00 8.83 3.33 0.78 21.00
0.00 8.39 0.00 8.83 3.33 0.78 21.00
0.00 4.85 0.00 8.78 8.78 0.45 20.00
0.00 4.85 0.00 8.78 3.78 0.45 20.00
0.00 9.34 0.00 9.33 9.33 0.82 22.00
0.00 9.34 0.00 9.33 9.33 0.32 22.00
0.00 17.83 0.00 8.30 8.80 1.68 21.00
0.00 17.83 0.00 8.30 8.80 1.68 21.00
PM
9/kg
PROBE PROSE LINE LINE
pre ut. post wt. pre wt. post wt.
9999
19.26 CCS-1A 0.0000 0.0031 0.0000 0.0014
19.99 CCS-1B 0.0000 0.0015 0.0000 0.0008
5.07 CCS-2A 0.0000 0.0010 0.0000 -0.0002
4.30 CCS -28 0.0000 0.0001 0.0000 -0.0003
12.78 CC3-3A 0.0000 0.0017 0.0000 0.0002
14.54 CCS-38 0.0000 0.0011 0.0000 -0.0002
3. 93 CC5-4A 0.0000 0.0024 0.0000 0.0004
3.37 CC5-4B 0.0000 0.0007 0.0000 -0.0001
37.32 CC5-5A 0.0000 0.0023 0.0000 0.0002
39.64 CCS-5B 0.0000 0.0036 0.0000 -0.0007
46.56 CCS-6A 0.0000 -0.0021 0.0000 0.0001
45.41 CCS-sa 0.0000 0.0019 0.0000 0.0008
28.45 CCS-7A 0.0000 0.0006 0.0000 0.0000
29.57 CCS-78 0.0000 0.0027 0.0000 -0.0009
3.95 CC3-8A 0.0000 -0.0026 0.0000 0.0003
4.03 CCS-SB 0.0000 -0.0021 0.0000 0.0007
Tank
Pressure
tor post
415
362
304
309
268
309
345
311
332
334
319
313
349
341
328
327
Front Back Rinse
PROSE LINE FILTER FILTER Residue
99999
0.0031 0.0014 0.0176 0.0000 0.0272
0.0015 0.0008 0.0234 -0.0004 0.0354
0.0010 -0.0002 0.0061 -0.0004 0.0077
0.0001 -0.0003 0.0064 -0.0010 0.0084
0.0017 0.0002 0.0141 -0.0001 0.0180
0.0011 -0.0002 0.0169 -0.0007 0.0264
0.0024 0.0004 0.0122 0.0002 0.0156
0.0007 -0.0001 0.0098 -0.0007 0.0161
0.0023 0.0002 0.0479 -0.0012 0.0707
0.0036 -0.0007 0.0494 0.0001 0.0744
-0.0021 0.0001 O.OS27 0.0011 0.0736
0.0019 0.0008 0.0497 -0.0002 0.0679
0.0006 0.0000 0.0245 0.0098 0.0555
0.0027 -0.0009 0.0394 0.0002 0.0490
-0.0026 0.0003 0.0062 -0.0001 0.0037
-0.0021 0.0007 0.0060 -0.0005 0.0086
Table 2.5 Country Comfort CC-150 RTF, NC VPI Test Results
2-7
-------
TABLE 2.6
CARBON MONOXIDE EMISSIONS
FOR ELEVATION VERSUS BURN RATE
Run#
Sweet Home
SH-31
B-3-ld
SH-2C
B-l-Sum"
B-2-Sumb
SH-8C
B-3-2d
SH-7C
B-3-3d
B-3-4d
SH-6C
SH-1C
SH-4C
SH-5'
Country Comfort
CC5-6C
A-3-ld
A-l-Sumb
CC5-5C
CC5-7C
A-2-Sumb
A-3-2d
CC5-le
A-3-3d
A-3-4d
CC5-3'
CC5-4C
CC5-8C
CC5-2<
Burn Rate
kg/hr
0.61
0.66
0.74
0.79
0.99
1.04
1.10
1.14
1.15
1.32
1.33
1.56
1.81
1.88
0.45
0.70
0.71
0.78
0.82
0.87
1.06
1.17
1.20
1.27
1.39
1.49
1.68
1.86
Carbon Monoxide
RTP,NC
Train Train Average
A B A and B
198.9 199.9
27.8 26.2
199.4
27.0
8.5
13.3
22.0
27.5
80.0
51.8
163.0 162.9 163.0
8.1
13.4
21.4
20.9
80.9
52.1
8.9
13.2
22.5
34.1
79.1
51.5
163.9
187.5
188.4
170.4
163.1
150.6
165.2
189.0
188.2
167.4
161.1
144.8
164.6
188.2
194.2 197.7 196.0
188.3
168.9
162.1
147.7
Carbon Monoxide
C.B., CO.
11.3
68.7
74.3
20.8
21.4
39.8
200.9
138.6
161.6
153.7
188.2
195.3
*The catalyst didn't light off this value is an outlier and is not used for Figure 2.2.
"Values at the end of 70-hour test using cordwood.
CRTP test series using 2 VPI trains and modified Method 28.
"Crested Butte test series using 1 VPI train and modified Method 28.
D123.40
241A.TAB
2-8
-------
VPI CO RESULTS AK-18 AND CC150
a b
U8 vs CRESTED 8UTTE
as
•^
o
kl
Q
X
O
o
2
Z
O
CD
5
o
220
210
200
190
180
170
160
150
140
130
120
110
100
90
80
70
60
50
40
30
20
10
0
0.4 0.6 0.8
1
1.2 1.4 1.6 1.8
BURN RATE KG/HR
O LAB AK-18 + LAB CC 150 O CRESTED BUTTE AK-18 £> CRESTED BUTTE CC150
a. outliers S-3A and 3B not used
b. results of cordwood tests not used
Figure 2.2 VPI Carbon Monoxide Comparison for Sweet Home AK-18 and Country
Comfort CC-150
2-9
-------
cr
METHOD iC EMISSION HATE CALCULATIONS
ItV MnuifUEfT HOME CilcuUtlon Information
Hod«t HolAK-11 l»iMtrlc,Z*Englshi 2.000
Lib ntmelES LAB CRESTED IUIIE, COLO.Oi, l-/nln, 2-/hr | 1.000
Tit 0«tilNOV-DEC,1919 Lib iltltud. (/() 18900.000 '
n>
•^
^
CD
r+
ffi
o
K> o>
' t^j
O i
oo
o
*-f
$
VPI COi
(j/hr)
21.02
04.4
0.470
1.009
304.403
750.215
0.00
150.20
3.70
152.13
5.54
7.54
0.74
21.70
12.2
0.470
1.009
759.103
1130.023
0.00
202.50
3.70
149.47
6.94
9.09
0.71
21.70
11.4
0.470
1.009
131.137
504.540
0.00
132.70
2.40
147.94
4.50
4.34
0.72
21.44
11.5
0.470
1.009
504.202
074.295
0.00
57.00
1.10
141.00
2.01
3.24
0.55
21.53
12.9
0.470
1.009
077.213
1250.042
0.00
320.10
4.30
152.04
11.22
13.54
0.09
21.71
; 01.1
''0.470
1.009
2470.741
4905.031
25.30
1109.50
21.40
149.47
7.05
9.20
0.79
10.900
1.400
7.500
9.030
41.700
21.74
70.4
0.470
1.009
313.925
420.555
0.00
141.70
3.40
141.33
3.14
7.11
1.02
21.41
13.7
0.470
1.009
422.307
1059.195
0.00
302.20
5.20
140.30
11.09
13.41
0.94
21.44
79.7
0.470
1.009
40.507
494.744
0.00
444.50
0.90
143.12
11.41
20.40
1.15
21.12
00.4
0.470
1.009
497.705
171.013
0.00
114.10
5.20
1(4.50
3.93
5.47
0.14
1-2-5 !
21.94
05.9
0.470
1.009
173.112
12(4.141
0.00
331.70
1.40
142.21
10. M
13.17
0.9}
1-2-4
21.14
17.4
0.470
1.009'
247.222
495.407
0.00
104.20
4.00
141.59
5.24
7.20
1.00
6-2-SUH
21.71
02.4
0.470
1.009
2414.771
4719.157
30.30
17(1.10
34.10
144.95
10.14
12.45
0.99
14.400
12.400
11.54
13.10
74.30
1-3-1 1
21.14
12.4
0.470
1.009
331.411
045.011
5.40
10.50
0.10
134.34
0.45
1.21
0.64
0.900
1.000
0.300
1.750
11.300
21.17
03.0
0.470
1.009
144.512
|]80.04i
0.70
30.70
1.90
132.11
1.37
2.37
.1.10
1.900
2.100
1.004
3.204
20.100
21.71
14.2
0.470
1.009
110.701
435.310
4.00
30.10
7.40
131.44
1.74
2.91
1.15
3.100
3.500
2.443
3.141
21.400
21.74
15.2
0.470
1.009
454.112
777.454
7.50
37.00
3.40
130.35
1.47
2.79
1.32
3.200
3.000
2.017
3.425
39.100
21.02
13.1
0.470
1.009
2034.934
3251.715
27.10
109.10
13.90
132.11
1.37
2.37
1.04
2.700
2.400
1.441
3.041
i 23.300
-------
HCTHCO SO
CALCULATIONS
§•
ts>
bo
O
g
&
5
*-notrlc,2>Englihi 2.000
Lib niMiES LAI CHESTED 8UTTE.COI.O Oi, |
-------
i
CD
to
VO
L!J
r^
Oq
tr
c§
C/>
to ^
i -4
(-» 5^
to rd
n
H
n
n
Cu
td
d
fb
??
c/i
£j
Co
HETHOO 30 EMISSION HATE CM.CUIAT IOHJ
Stv ranuiHAUGHEt CiUulnlon Information
Modi 1 Nolf-173E 1'«Klrlc,2«Engtlhl 2.000
Lib mmtlES LAI CHESTED BUTTE.COLO. Oi, 1-/mln, 2-/hr I 1.000
Tit Oll«lKOV-OEC,1909 Lib lUltud. (( t ) 18900 .000
Pb(_Hg)l 21.80
Tndvglt 93. (
dHdvg)! 0.550
DCH, T 1 1.046
OGHI 1 179.001
OGHf t 554.140
•*«rnt)l 0.00
ng(/U1)i 601.60
mg(Mf2)l 1.30
Oi(ivg) I 1(0.90
ElUg/hr)! 19.09
EMH5H) 1 21.05
1.06
VPI ACTi
(t/Kr)
VPI by VMi
TO 50 (i/hr)
VPI by ESi
TO 5Q (g/hr)
VM liy IS!
TO 5k (s/hr)
VPI CO-'
21.12
94.0
0.550
1.0(6
359.219
9I(.10(
0.00
131.20
5.20
1(6.46
(.17
6.77
1.09
21.71
11.7
0.550
1.0(6
916.604
1270.121
0.00
290.60
7.00
1(3.26
10.00
12.30
0.97
21.70
15. 5
0.530
1.046
272.403
625.579
0.00
265.10
(.50
1(9.50
9.31
11.60
0.06
21.64
1S.(
O.SSO
1.046
626.916
912.312
0.00
(11.90
1.60
153. (7
17.32
19. (1
0.15
21.53
15.5
0.550
1.0(6
915.020
13(1.772
0.00
296.70
6.20
1(7.31
10.29
12.60
0.79
21.71 21.76
11.1
0.550
1.0(6
3539.233
5611.105
56.30
2011.10
39.10
1(7.15
12.23
14.54
0.94
20.100
15.000
14.549
16.237
125.600
13.0
0.550
1.046
354.610
6(9.952
0.00
329.00
7.30
1(6.75
13.33
15.12
1.03
21.61
15.5
0.550
1.0(6
650.952
1043.035
0.00
379.20
7.10
1(1.11
10.80
13.12
0.10
121.66
83.3
0.550
1.0(6
61.5(1
(11.276
0.00
324.00
12.30
144.45
15.21
17.50
1.14
21.12
13.1
0.550
1.046
(14.601
135.450
0.00
(01.00
11.00
140.73
13.35
15.64
1.13
21.94 21.14
17.2
0.550
1.046
137.003
1117.341
0.00
2M.20
8.20
146.16
10.06
12.36
0.17
11.0
0.550
1.0(6'
109.907
422.943
0.00
134.40
5.20
1(1.70
6.91
9.06
0.71
21.71 21.16
65.0
0.550
1.046
2315.621
44(i,004
54.90
2055.10
31.10
143.71
12.27
14.51
0.97
25.400
1 7 . 100
17.12(
19.516
H2.300
75.7
0.550
1.0(6
((1.912
737.771
0.00
372. (0
11.10
140. (9
14.48
14. 73
1.34
21.17
15.1
0,550
1.046
739. 6H
10H.340
0.00
1(7.00
6.90
152.17
4.44
t.S(
1.09
21.71 21.76 21.96
M.I
0.550
1.0(6
35.232
124.543
0.00
226.30
6.80
129.27
1.32
10.77
1.43
K.I
0.550
1.0(6
325.312
622. 40(
0.00
424.00
7.90
137.11
16.19
11.35
0.98
83.8
0.550
1.046
623.102
915.913
0.00
212.40
1.30
136.72
1.21
10.52
1.17
21.94 21.10
84.3
0.550
1.046
916.923
1209.913
0.00
(91.50
7.00
137.87
18.84
20.16
0.92
M.6
0.530
1.0(6
210.902
504.592
0.00
111.40
5.10
131.21
7.U
9.31
0.98
21.85
13.2
0.350
1.0(6
3293.197
3349.623
67.70
2055.00
53.10
138. U
11.17
14.11
1.13
16.600
12. (00
11.558
13.110
1(8.900
»l*> Ho.tC-1-1 C-1-2 C-1-3 C-1-( C-1-5 C-1-6 C-1-SUH C-2-1 C-2-2 C-2-3 C-2-4 C-2-5 C-2-6 C-2-SUH C-3-1 C-3-2 c-3-3 C-3-4 C-3-5 C-3-6 C-3-7 C-3-SUH
-------
tsi
METHCO 50 EMISSION HATE CALCULATIONS
flv nruiASHLEY Cilculitlon Information
Hod. I KOI OVAL 1-/Mtrlc,2>Englihi 2.000
Lib niMifl LAI CHESTED lUTTE.COLO. at, l"/mln,2-/hr i 1.000
Js>
h-l
o
>
In
hr1
e
f+.
$
£L
!"• *
P
?>
a
0>
^i
M*
W
el
Tit Oltll»OV-OEC<1919
Kin Ho.lO-1-1
fb(_Hg)i 11.10
T«(iV|)i 15.9
dX(ivg)i 0.100
OCX, Y 1 0.974
OCHI t 419.002
OGMf i 007.291
•9(frnt)i 0.00
KtCmnt 1045.00
»«C»I«>| 23.50
Oi(ivg) i 131.11
I*fl/hf)l 33.41
IKHJH) t 33.49
1.49
*»•• l^T.
0-1-2 0-1-3
21.12
11.4
0.100
0.974
109.402
1197.242
0.00
559.10
21.40
130.41
17.12
19.41
1.71
21.70
17.2
0.100
0.974
199.102
390.154
0.00
523.00
10.00
122.19
13.13
17.35
1.55
Lib iltltudi (ft)t0900.000
0-1-4 0-1-5
21.70
05.9
0.100
0.974
511.504
911.911
0.00
174.10
20.50
121.71
25. 11
21.92
1.09
21.14
15.9
0.513
0.974
970.025
1331.710
0.00
1403.30
33.10
129.93
43.07
41.35
1.42
0-1-1 0-1-SUH
21.53 21.71
15.1 11.5
0.112 0.111
0,974 0.974
354.001 3111.041
719.304 5113.407
0.00 215.50
191.10 5101.00
24.50 152.70
121.49 129.41
20.21 21.14
22.11 27.75
1.41 1.45
In *nft
0-2-1
21'. 71
14.2
0.111
0.974
701.104
1110.191
0.00
515.40
21.10
121,71
20.95
22.15
2.14
0-2-2
21.10
17.1
0.150
0.974
111.101
511.021
0.00
1074.30
29.40
121.51
21.19
27.91
1.45
0-2-3 0-2-4
21.11
14.7
0.119
0.974
571.714
1010.014
0.00
1295.40
49.00
121.11
31.11
32.04
2.02
21.02
14.1
0.109
0.974
31.403
431.417
0.00
1171.00
29.70
131.70
34.01
34.00
1.43
0-2-5
21.94
19.2
0.171
0.974
431.127
131.413
0.00
1233.40
31.50
129.10
35.42
33.32
1.47
0-2-1
21.14
19.1
0.173
0.974
019.507
1104.JU
0.00
729.70
24.50
121.71
11.53
31.92
1.12
0-2'SUH
21.71
il.4
O.ilO
0.974
2779.011
3090.974
414.10
4019.40
1»2.30
127.40
32.41
32.19
1.17
•
0-3-1 0-3-2
21.11
77.1
0.177
0.974
112.010
459.411
0.00
1217.10
49.40
112.17
45.19
41.42
2.14
21.07
'll.l
0.193
0.974
441.243
000.221
0.00
1197.10
37.40
132.20
41.91
40.41
1.91
0-3-3 0-3-4 0-3-5
21.70
94.4
0.591
0.974
001.314
1123.910
0.00
.132.00
42.00
120.90
21.99
23.11
1.02
21.71
05.4
0.100
0.974
123.010
447.342
0.00
301.10
11.10
• 125.39
10.79
11.11
0.97
21.91
05.9
0.141
0.974
440.703
001.244
0.00
1339.20
72.30
124.59
42.10
40.90
1.91
0-3-1 0-3-7 0-3-SUM
21.94
is.:
0.171
0.974
007.701
1144.593
0.00
541.10
17.30
133.44
19.11
21.11
1.02
21.10 21.15
05.9 14.4
0.112 0.151
0.974 0.974
145.105 2921.101
415.191 5211.941
0.00 411.50
151.40 5939.50
32.10 212.10
132.17 121.71
23.39 31.51
24.91 31.94
1.15 1.14
1O iftft
CD
HJ VPI by VPI i
0> TO SO (g/hr)
^ Wl by ESi
£? TO SO (g/hr)
w VPI by ESi
TO 5H (j/hr)
VPI COi
1
r)
r)
r)
ir)
1.1*1
25.500
27.151
29.123
100.400
0.1.2 D-1-l D-1-4 D-1-5 0-1-1 0-1-SUH 0-2-1
24.700
31.131
11.200
JOS. 700
0-2-2 0-2-3 0-2-4 0-2-5 0-2-4 0-2-SUH D-3-1 D-3-2
21.200
27.914
• 29.924
222.700
D-l-3 D-3-4 0-3-5 0-3-1 0-3-7 0-3-SUM
-------
RUN t
A-1
8-1
C-1
0-1
A-2
B-2
C-2
0-2
A-3-1
A-3-2
A-3-3
A-3-4
B-3-1
8-3-2
8-3-3
B-3-4
C-3
0-3
RUN *
UOOO DATE
RUN * HEATER RETRIEVED
MODEL
A-1 CC150 11-14-89
B-1 AK-18 11-14-89
C-1 S173E 11-14-89
0-1 ASHLET 11-14-89
A-2 CC150 11-20-89
B-2 AK-18 11-20-89
•* C-2 S173E 11-20-89
0-2 ASHLET 11-20-89
A-3-1 CT.150 11-28-39
A-3-2 CC150 11-29-89
A-3-3 CC150 11-30-89
A-3-4 CC150 12-01-89
B-3-1 AK-18 11-28-89
••• B-3-2 AK-18 11-29-89
B-3-3 AK-18 11-30-89
B-3-4 AK-18 12-01-89
***• C-3 S173E 12-04-89
**** 0-3 ASHLET 12-04-89
Tank
C02
X
Tank
CO
X
Tank
02
X
TOTAL
CATCH
3 (A)
FUEL
TTPE
•MIX
•HIX
•MIX
•MIX
•MIX
•MIX
•HIX
•MIX
0. FIR
0. FIR
D. FIR
0. FIR
0. FIR
0. FIR
D. FIR
0. FIR
HIX
MIX
PH
g/hr
LOADED
FUEL
wet kg
57.5
63.9
76.3
116.8
71.3
31.2
78.7
141.2
9.3
13.3
14.5
14.6
7.5
14.5
12.5
16.4
89.0
139.0
CO
g/hr
FUEL MC
dry X
12.8
12.2
12.8
11.8
16.8
17.5
15.7
20.5
21.3
21.9
21.2
20.3
20.3
22.7
20.3
20.0
12.6
19.5
CO
9/kg
EOKJV INITIAL FINAL TOTAL EOIHV Fl"Al
COAL BURNEU HOUIl HOB S4MPLINS BU*" ™N><
BED FUEL METER METER TIME RATE TE.MP
kg wet kg hr hr hr dry kg/hr C
0 57.52 0.00 72.00 72 0.71 22
0 63.87 O-.OO 72.00 72 0.79 22
0 76.34 o'.OO 72.00 72 0.94 22
0 116.76 0.00 72.00 72 1.45 21.5
0 71.30 0.00 70.00 70 0.87 25.5
0 81.19 0.00 70.00 70 0.99 25.5
0 78.65 0.00 70.00 70 0.97 24
0 141.16 0.00 70.00 70 1.67 24'
0 9.25 0.00 10.82 10.82 0.70 20
0 13.34 0.00 10.35 10.35 1.06 28
0 14.51 0.00 10.00 10 1.20 23
0 14.56 0.00 9.50 9.5 1.27 21
0 7.53 0.00 9.53 9.53 0.66 21
0 14.47 0.00 10.77 10.77 1.10 28
0 12.47 0.00 8.95 3.95 1.15 28
0 16.42 0.00 10.37 10.37 1.32 24
0 89.04 0.00 70.00 70 1.13 25
0 138.98 0.00 71.00 71 1.64 25
PM
9/kg
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To look at elevation effects on the emission rates of the Sweet Home AK-18
and the Country Comfort CC-150 the emission rates from the 1988 study at Mt.
Mitchell using Method 28 and 5G (elevation ~ 5800 feet) is compared with the tests
done at the RTF laboratory (elevation ~ 300 feet) and at Crested Butte (elevation
~ 8900 feet). The tests at RTF and Crested Butte were in conjunction with the VPI
study and were done using a modified Method 28 lasting approximately ten hours
for each run. It should be noted that the limited number of tests and bum rates at
Crested Butte tend to show the trend line more than the other two. This is most
apparent with the CC-150. Figure 2.3 shows the results for the AK-18 while Figure
2.4 shows results for the CC-150. The actual numbers and formulas used to
generate the graphs can be found in Appendix E. It can be seen based on the fairly
limited number of tests for each condition that elevation, while affecting obtainable
burn rates, does not significantly affect emission rates for a given burn rate.
The second question as to the effect of burning regular cordwood using normal
house heating operating procedures shows a major affect to the catalytic AK-18's
emissions as shown in Figure 2.5. Figure 2.6 shows the results for the CC-150. The
cordwood results are skewed by two relatively low emission rates at low burn rates.
Without these two, it appears that cordwood would give approximately the same
expected emission rates as Method 28. Figure 2.7 depicts the results for the
Haughes S-173 E. The RTF lab baseline test results are from the woodstove's
baseline testing for use in the laboratory accreditation program which use Method
28. It can be seen that cordwood and elevation doesn't appear to significantly affect
emissions for that woodstove.
Figure 2.8 shows the emission rates for the Ashley Oval, a woodstove which was
typical of woodstoves used in Crested Butte prior to the 1989 heating season.
Table 2.12 provides a listing of the individual tests for which a problem was
encountered (C-3-3 the fan broke), or there was a deviation from the method (SH-1
Trains off for 20 minutes between fuel cribs). Most of the method deviations were a
failure to have the sampling proportionality ratio between 90 and 110%. It should
be noted that only one of the deviation (SH-3) would have significantly affected the
test results if it were included. Since it was a obvious outlier it was not used.
123.40
1A.RPT 2-15
-------
ce
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26
24
22
20
18
16
14
12
10
8
6
4
2
0
AK-18 5G ADJUSTED TO 5H
LAB— CRESTED BUTTE—MT MITCHELL
,„. HltCHEU.
0.4
0.8
1.2
1.6
D AK-18 5G(ADJ) LAB
BURN RATE (KG/HR)
LAB BEST FIT O CRESTED BUTTE
X MT. MITCHELL M M BEST FIT
2.4
C 8 BEST FIT
a. outliers SH-3A and SH-3B are not used
Figure 2.3 Emission Results for Sweet Home AK-13 at Different Elevations while
Burning Douglas Fir Cribs
2-16
-------
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24 -
22 -
20 -
18 -
16 -
14 -
12
10
8
6
4
2
CC150 5G ADJUSTED TO 5H
LAB—CRESTED 8UTTE—MT MITCHELL
0.4
D CC150 (5G ADJ) LAB
0.8
1.2
1.6
BURN RATE (KG/HR)
LAB BEST FIT O CRESTED BUTTE
X MT. MITCHELL M M BEST FIT
2.4
C 8 BEST FIT
a. run A-3-1 with a burn rate of 0.70 kg/hr is off scale
at 28.8 g/hr
Figure 2.4 Emission Results for Country Comfort CC-150 at Different Elevations
Burning Douglas Fir Cribs
2-17
-------
X
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O
in
26
24 -
22 -
20
18
16 h
14
12
10
3
6
4
2
AK-18 CORDWOOD vs 5G(ADJ)/28
LAB—CRESTED BUTTE
0.4
0.8
1.2
1.6
2.4
D AK-18 5G(ADJ) LAB
BURN RATE (KG/HR) ~
LAB BEST FIT o CRESTED B. CORDWOOD
v C 8 5G(ADJ)-28 C8 5G(AOJ) BEST FIT
C B BEST FIT
Figure 2 5 Emission Rates Sweet Home AK-18 Normal Burning of Cordwood
Versus Modified Method 28
2-18
-------
I
2
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CC 150 CORDWOOD vs 5G(ADJ)/28
20 h
15 \-
10 h
5h
LAB—CRESTED BUTTE
i i i i i ' 1 1
2.4
D CC 150 5G(AOJ) LAB
BURN RATE (KG/HR)
LAB BEST FIT O CRESTED B. CORDWOOD
x C B 5G(ADJ)-28 CB 5G(ADJ) BEST FIT
C B BEST FIT
Figure 2 6 Emission Rates Country Comfort CC-150 Normal Burning of Cordwood
* ' Versus Modified Method 28
-------
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45
40
35
30
25
20
15
10
HAUGHS S-173E 5G(ADJ) VALUES
CORDWOOO vs METHOD 28
a a
0.4
0.8
1.2
1.6
2.4
Q £8 DAILY 5G(ADJ)
BURN RATE (KG/HR)
C8 DAILY BEST FIT o LAB BASELINE
X CB TEST SUMS CB SUMS BEST FIT
2.8
3.2
BASELINE BEST FIT
Figure 2.7 Emission Rates Haughes S-173E Normal Burning of Cordwood at 8900
Feet Elevation Versus Method 28 at 300 Feet
2-20
-------
ASHLEY CORDWOOD 5G(ADJ)
CRESTED BUTTE
CK
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45
40
35
30
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20
15
10
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O ASHLEY 5G(ADJ) CB
BURN RATE (KG/HR)
- DAILY BEST FIT
SUMS BEST FIT
ASHLEY 5G(ADJ) SUMS
Figure 2.8 Emission Rates/Ashley Oval Emission Rates for Normal Cordwood
Burning
2-21
-------
Table 2.12
TEST SPECIFIC METHOD DEVIATIONS AND RESOLUTIONS
TESTING PHASE ONE RTF. NORTH CAROLINA
Test#
SH-1
SH-3
SH-6
SH-7
Sweet Home AK-18
Description of deviation
First crib weight went to zero
before another crib was ready.
The catalyst did not light off
during the first crib.
A drop of condensate was in the
VPI-6A probe's swageloc connector.
Found the drop of condensate
in the VPI-7A probe.
Effect on Results
and Resolutions
Results not significantly
effected. Turned all
sampling trains off (20
minnt.es) until next crib
was ready
VPI vs 5G results not
effected. Emission rates
were not used for cordwood
to Method 28 comparisons.
Results not significantly
effected. Corrected the
probe's final weight.
Results not significantly
effected. Corrected the
probe's initial weight.
Country Comfort CC-150
Test # Description of deviation
CCS-1 Small tank leak for VPI-1A.
CC5-3 Small leak at evacuating
quick-connect.
Effect on Results
and Resolutions
Results not significantly
effected. Resealed the
tank before using again.
Results not significantly
effected fixed the leak.
123.40
1A.RPT
2-22
-------
Table 2.12 (Continued)
TESTING PHASE TWO CRESTED BUTTE, COLORADO
Sweet Home AK-18
Test # Description of deviation
B-3-4 1 Proportionality Ratio over 110%
Effect on Results
and Resolutions
Results not significantly
effected.
Country Comfort CC-150
Test#
A-l
A-l-5
A-2-3
A-2-4
A-3-1
Description of deviation
VPI probe broke at the test
series end while trying to
remove it from the stack.
The stove would not burn
properly.
Tunnel flow average
125.7 DSCFM.
Tunnel flow average
125.6 DSCFM.
Secondary didn't light
off properly for first
9 hours of test.
Effect on Results
and Resolutions
The probe's interior was
brushed and rinsed
with acetone. Did
not significantly
effect the results.
The by-pass was opened
for last y/i hours of
test day to promote
burning. Insulation was
found to be blocking the
secondary air. The insu-
lation was moved to
prevent blockage.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
123.40
1A.RPT
2-23
-------
Test^
C-3-3
C-3-3
Table 2.12 (Continued)
Haushe's S-173E
Description of deviation
Dilution tunnel fan broke
in middle of test day.
1 Proportionality ratio
of 88%.
Effect on Results
and Resolutions
Results not significantly
effected. Turned the trains
off and emptied stove.
Fixed the fan restarted the
trains and the stove.
Results not significantly
effected.
Test#
D-l
D-l-2
D-l-3
D-l-3
D-l-4
D-l-5
D-l-6
D-2-1
D-2-2
D-2-3
D-2-5
Ashley Oval
Description of deviation
VPI probe broke at the
test series end.
2 Proprotionality ratio
over 110%
2 Proprotionality ratio
over 110%
Tunnel flow average
122.2 DSCFM
1 Proprotionality ratio
over 110%
2 Proprotionality ratio
over 110%
2 Proprotionality ratio
over 110%
Tunnel flow 125.8 DSCFM
3 Proprotionality ratio over 110%
1 Proprotionality over 110%
Tunnel flow 123.2 DSCFM
1 Proprotionality ratio over 110%
1 Proprotionality under 90%
2 Proprotionality over 110%
Effect on Results
and Resolutions
Results not significantly
effected. The probe's
interior was brushed
and rinsed with acetone.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
Results not significantly
effected.
No Results not significantly
effected.
No Results not significantly
effected.
123.40
•1A.RPT
2-24
-------
Table 2.12 (Continued)
Ashley Oval (Continued)
Test # Description of deviation
D-3-1 1 Proprotionality over 110%
D-3-2 2 Proprotionality over 110%
D-3-5 2 Proprotionality over 110%
1 Proprotionality under 90%
D-3-7 1 Proprotionality over 110%
Effect on Results
and Resolutions
No results not significantly
effect.
No results not significantly
effect.
No results not significantly
effect
No effect.
Ashley Footnote:
The burn rate could not be controlled. When the burn rate was very high the
dilution tunnel temperature also was quite high. This higher temperature caused
the fan to pull less runnel gas at standard conditions than it would at lower
temperatures. The lower tunnel flow rate (DSCFM) caused the proportionality
ratio's to be to high.
123.40
1A.RPT
2-25
-------
SECTION 3.0
-------
SECTION 3
TEST FACILITIES AND METHODS
Two test facilities were used for the EPA Method 5G versus the VPI Sampling
Method Comparison study. They were Engineering-Science's Wood Stove Test
Laboratory Research Triangle Park, North Carolina, and a leased facility located in
Crested Butte, Colorado. For cordwood versus EPA Method 28 at elevation
comparison purposes, results from the 1988 Mt. Mitchell North Carolina test
program are included for the Sweet Home AK-18 and Country Comfort CC-150.
Figures 3.1 and 3.2 presents the RTP wood stove laboratory. Figures 3.3 and 3.4
show the Mt Mitchell facility. While Figure 3.5 shows a overview of the Crested
Butte facility. Figure 3.6 shows the individual stove's test configuration for the
Crested Butte test series.
Test Methods Used For Phase One (Method 5G versus VPI Method^
Modified Method 28
Method 28 was strictly followed except for the following modifications. Dr.
Jaasma of VPI determined that the VPI sampler should be operated at a maximum
flow rate of 60 rnilhliters per minute. This was based on their maximum flow rate
during prior testing. The desired sample volume, of 34 liters, is approximately one
half the vacuum tank's capacity. If the sample is too small there are problems with:
1. Removing the stack gas from the evacuated tank for analysis.
2. Very low weights of the individual sample components.
If the sample is too large, when the vacuum becomes too low, the valve no
longer acts as a critical orifice, and the sample flow rate will decrease. This will
cause a biased sample.
Based on these considerations, the sample flow rate and total sample volume,
was determined for each test run should be as near to 10 hours in length as possible.
The maximum crib weight for the AK-18 is 7 kilograms, while the CC-150 is 5.3
kilograms. The maximum burn rate sustainable for the AK-18 would be less than
0.7 kilograms per hour over 10 hours, for one crib of maximum weight.
Therefore; while the start of a test was the same as for a stove certification test
when the crib weight was reduced to zero a new crib (or partial crib as needed to
reach zero at the end of 10 hours) was added If it was determined after 9 hours the
crib would not reach zero in 10 hours, the primary air was fully opened to increase
the burn rate.
The test was ended when the final crib, or partial crib, weight had been reduced
to zero.
123.40
1A.RPT 3-1
-------
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Hood Exhaust
Inslrumanlallon Area
Scale Weights and
Anemometer i
Wood Prep. Area
Truck Dockwllh
Overhead Door
Hood
TC Swilcli
Box Sampling Ports
Room
Temperature T/C
IBM PC
Computer
Calibration
Gas Cylinders
Controlled Wood
Slorago Conlainer
Blower
Analytical
Balance
Sample
Recovery/
Clean-up
Area
Velocity
Traverse Ports
Wood Moisture
Meter
COUNTRY COMFORT
CC-150
VPI TEST SERIES
SWEET HOME
AK-18
VPI TEST SERIES |
Clean Glass Storage
Aneroid
Barometer
Mercury
Barometer
Legend:
• Dilution Tunnel «1
• Dilution Tunnel 112
E/S WOOD STOVE
TEST FACILITY
TOP VIEW
-------
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Instrumentation
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Truck Dock with
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SWEET HOME
AK-18
VPI TEST SERIES
COUNTRY COMFORT
CC-150
VPI TEST SERIES
velocity Traverse
Ports
> False Celling |*',
Damper
/ Blower
Hood
IBM PC
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Clean
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Sample Recovery/ Storage
Clean-up Area
Legend:
I I - Dilution Tunnel «1
I»i1 . Dilution Tunnel fl2
Humldlller
Traverse
Ports
Sampling Slove Test
Ports Wood In
Sample Controlled
Ports Container
E/S WOOD STOVE
TEST FACILITY
SIDE VIEW
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Dilution
Gas Sampling Tunnel QM Samp|a
Anemometer I ''0°a x a^ Moisture
Scale Weights / \ Knock-out
Gas Sampling Callbralion Gases
Control Module
Sample Train B / CO, /CO Monitor
Ryder Truck
Door
Truck Cab
Storage
Electric Scaffolding
Healar Enclosure
MT. MITCHELL
STOVE TEST FACILITY
TOP VIEW
-------
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Scaffolding
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Dilution
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Hood
A
Plastic Skylight Area
Dilution
Plywood and
Plastic Enclosed Area
1 I
Dilution
Tunnel
Pilot
and T/C
Gas Sampling
(Moisture Knock-
out and filler)
Calibrallon
Gases
Gas Sampling Control Module
Ryder Truck
Barometer
\
ICO, /CO Monitor
I O2 Monitor
Room
Temperature
T/C
Stove
Scale
Kerosene
Healer
Electric Healer
\
Sampling
Ports Sampling Train
Moisture Knock-out
Table Top /
Sample Train
an-up Araa
Electric Heater
Truck Cab
MT. MITCHELL
STOVE TEST FACILITY
SIDE VIEW
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72"
168"
VTI stazix pom
Figure 3.6 Test Configuration For Individual Stove At Crested Butte
3-7
-------
Method 5G
Method 5G was strictly followed for this test series. The dual sampling trains
were operated continuously from just before the first crib was added until the last
crib or partial crib weight was reduced to zero.
Figure 3.7 is a schematic of the Method 5G sampling train as used for this test
program. Figure 3.8 depicts the dual 4" filter holder and probe assembly. Figure 3.9
depict the vertical duct/dual Method 5G trains as used for the AK-18. While Figure
3.10 shows the dual tram/horizontal duct as used for the CC-150.
VPI Sampling Method
Figure 3.11 provides a schematic of the VPI sampling train as used by
Engineering-Science for this test program.
Figure 3.12 depicts the VPI sampler as used in the homes of Crested Butte. It
can be noted that the major difference is that the in home sampler is turned on and
off based on a set stack temperature. Whereas the VPI samplers for this program
were turned on manually to run simultaneously with the Method 5G sampling trains.
Sampler Setup:
Evacuate sampler to at least 0.3" Hg absolute.
Renew the desiccant (*Drierite).
Weigh connector table, Teflon line and probe (use anti-static device).
Assemble pre-weighed filters, line and probe (line should impinge against
the inside wall of the trap about 1 to 2 inches above the trap's bottom.)
Install filter set and perform leak check at 4 inches water (leak rate needs
to be less than 1 inch per minute).
Set sampler flow rate using rotometer.
Make sure 2 way valve is closed.
Cap probe.
Recheck sampler's pressure must be less than 0.25" Hg absolute.
Record all readings on Data Sheet (Figure 3.13).
Sampler Deployment
Place sampler in position (as far from stove as possible).
Drill holes for VPI probes and a optional thermocouple at 12 inches above
stove collar.
Place probe in position for sampling (probe position for Crested Butte test
series is shown in Figure 3.14).
Open two way valve two start sampling.
Sampler Retrieval
Close two way valve.
Remove probe from stack.
Cap probe.
Move sampler to recovery area.
123.40
1ARPT 3-8
-------
Dual Filter Holder
with Thermocouple
In the Spacer
B=
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Thermocouple
3/8" Teflon Tube
with Glass Sockets
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H2O H20 Empty Silica
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Bypass Valve
Pilot Manometer
Air Tight
Pump
Vacuum
Line
. Vacuum
Gauge
To The
Stove Stack
Flue Draft
Manometer
To The
Dilution
Tunnel
Pilot
Manometer
Figure 3.7 Engineering-Science Method 5G Sampling Train
3-9
-------
Glass Front
Filter Bell
Glass
Spacer
14"
Glass Probe
Front Fritted Glass and
SIHcone Rubber Filter Support
Thermocouple
Glass Back
Filter Bell
Glass Front
Filter Bell
Glass .
Spacer
Glass Back
Filter Bell
Back Fritted Glass and
Silicone Rubber Filter Support
14"
10"
Water Cooled Probe
Water In
Front Fritted Glass and
Silicone Rubber Filter Support
Thermocouple
Back Fritted Glass and
Silicone Rubber Filter Support
•-Water Out
Figure 3.8 Engineering-Science Method 5G Filter Holder/Probe Assembly
3-10
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SAMPLE TANK
70 LITER
L
QUARTZ PROBE
FLOW
'CONTROLLER
METERING VALVE
VACUUM CAUCE
I TV
- 2-WAK VALVE
QUICK CONNECT
(FOR EVACUATION, PRESSURE MEASUREMENTS, SAMPLE RECOVERY)
"B" Sample^
Probe
T/C
Stove
Stack
VPI SAMPLE TRAIN SCHEMATIC
DUAL VPI TRAIN
STACK SCHEMATIC
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QUARTZ PROBE
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DUAL 47mm
FILTER UNIT
SOLENOID VALVE
I I
METERING VALVE \
FLOW
CONTROLLER
GAUGE
TEMPERATURE.
TIMER CONTROLLER
2-WAY VALVE
QUICK CONNECT
(FOR EVACUATION, PRESSURE MEASUREMENTS. SAMPLE RECOVERY)
THERMOCOUPLE
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED
DATE RETRIEVED_
TEST LOCATION_
SAMPLER SNi?
(HG BAROMETER UNCORRECTED)
PRETEST B.P (IN HG)
TANK
(—IN HG) TEMP.
PROBE
LINE
CONDENSATE_
FILTER;? 1
FILTERS
TOTAL (MG) _
(C)
TORR ABSOLUTE_
POSTTEST B.P._
TANK
(IN HG)
(—IN HG) TEMP.
(C)
TORR ABSOLUTE
PRETEST LEAK CHECK
START
(IN HBO) FINAL
POSTTEST LEAK CHECK
START (IN H20) FINAL
(IN H20) LEAK RATE
(IN H2) LEAK RATE
RUN*
TEST TIME_
STOVE ID
(MIN.)
WOOD SPECIES
WOOD MOISTURE (Z DRY)_
WOOD MOISTURE (% WET)_
WOOD CONSUMED (LB)
(KG)
SAMPLE FLOW RATE PRETEST
ROTQHETER =(ML MIN)
POSTTEST
ROTAMETER
•(ML MIN)
_(IN H20 MIN)
(IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(Z)
RUN COMMENTS:
CO(Z)
02(2)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
MIN.
MIN.
MIN.
DELTA
PROBE+FITTING
SAMPLE LINE
CONNECTOR
Figure 3.13 Data Sheet Used For VPI IN-Situ Testing
3-15
-------
Dilution Tunnel
Filter
Holder
Impinger
Box
Umbilical
Line to
Meter
Box
Figure 3.14 Method 5G Sampling Train Configuration As Used At Crested Butte
3-16
-------
Sample Recovery
Measure and record sampler leak rate at 4 inches water.
Measure and record sampler pressure and temperature.
Calibrate CO/CC>2 and 62 §as instrumentation.
Fill gas sample bag by pumping sampled gas from the evacuated tank.
Attach gas bag to manifold for CO/CXI^ and C>2 analyzers. Record
reading for each gas.
START TANK EVACUATION FOR NEXT TEST.
Remove filters put in petri dishes and place in desiccator.
Scrape "O" rings recover with acetone rinse into condensers sample.
Remove stainless steel connector tube from condenser stopper
(acetone rinse into condenser) place connector in desiccator.
Flush probe and Teflon line into condenser with approximately 50 mL
acetone.
Place all acetone rinses into a beaker, allow acetone to evaporate and
then desiccate the beaker.
Disconnect probe and line from condenser, acetone rinse condenser.
Clean outside of probe and line using razor blade and acetone wipe
(do not save).
Connect probe and attached Teflon line to nitrogen or pure air
source.
Flow nitrogen, at about 0.5 liter minute for at least a half hour,
through probe and line assembly.
Disconnect probe and line from nitrogen and wipe with acetone.
Disconnect line from probe, coil line to fit in balance.
Sample Weighings
Probe and line use anti-static device and weigh separately than
reattach to nitrogen purge for at least 10 minutes before reweighing.
The weighing is complete when consecutive weights vary by less than
0.25 milligrams.
Weigh filters after desiccation, weighing is complete when consecutive
weights vary by less than 0.2 milligrams over 2 hours.
Weigh acetone rinse beaker, weighing is complete when consecutive
weights vary by less than 0.5 milligrams over 4 hours.
Weigh the connector, weighing is complete when consecutive
weighing vary by less than 0.2 milligrams.
Sample Calculations
All VPI values calculated with 11-28-89 corrected formulas as
supplied by Dr. Jaasma.
23.40
A.RPT 3-17
-------
CRESTED BUTTE TEST PROTOCOL
A overview of the tests conducted at Crested Butte is shown in Table 3.1.
Modified Method 28
The Sweet Home AK-18 and Country Comfort CC-150 were each tested 4
times using the same modified Method 28 procedures as described for the RTF tests
with the following exceptions:
The stove wall temperatures were averaged electronically before
reading and recording.
The test readings were checked at 15 minute intervals and recorded
every 60 minutes except for the final reading which was taken when
the final crib weight was reduced to zero.
Tne stove stack and tunnel were cleaned at the start of the test
program but not before this test series.
Cordwood Test Methods
Testing was started before the kindling was lit on the first day of each test
series. Other days the sampling trains were started before any wood was added to
the stoves. The stoves were loaded with wood at the end of each test day to allow
them to burn overnight and be ready to start testing in the morning. The primary air
and other operating parameters were varied to approximate normal usage of a wood
stove. The stoves were adjusted and loaded in a random fashion to attempt to
duplicate how a average home owner would operate a wood heater. In general, the
heater was at maximum at the start of each day - than at lower rates for the majority
of the day. Wood was loaded into the stoves as required.
Each wood stove was tested using one Method 5G sampling train and
one VPI sampling train.
Determination of cordwood moisture was done using a Delmhorst
Model RDX01 with a 26E electrode.
The cordwood burned during the tests was a mixture of spruce
and pine which were taken from the forest as standing
deadwood. The standing deadwood had approximately 8-12%
moisture on a dry basis. During the second and third test
series the standing deadwood was mixed with some Douglas fir
of approximately 30-55% moisture on a dry basis. The
Douglas fir's moisture was high because the firewood came
from the remains of live trees cut for lumber. The cordwood
supplier indicated that this mixture was normal fire wood for
Crested Butte.
Dilution Tunnel and Stack - Flow and Cleaning:
Tunnel flow was determined in each tunnel and adjusted to be
between 126 and 154 SCFM (with a cold stove) before each
test series. The pitot was positioned at the average point
123.40
1A.RPT 3-18
-------
TABLE 3.1
CRESTED BUTTE TEST PROGRAM OVERVIEW
CC-150
AK-18
S-173E
Ashley
CC-150
AK-18
S-173E
Ashley
A-173E
Ashley
CC-150
AK-18
TEST SERIES
A-l
B-l
C-l
D-l
A-2
B-2
C-2
D-2
C-3
D-3
A-3-1
A-3-2
A-3-3
A-3-4
B-3-1
B-3-2
B-3-3
B-3-4
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Cordwood
Douglas
Fir Test
Douglas
Fir Test
Sample
Recovery
5G
Filters daily
Rinse end of
series
Filters daQy
Rinse end of
series
Filters daily
Rinse end of
series
Filters daily
Rinse end of
series
Filters daily
Rinse end of
series
Filters dafly
Rinse end
series
Filters daily
Rinse end
series
Filters daily
Rinse end
series
Filters daily
Rinse end of
series
Filters Dafly
Rinse end of
series
Filters and
rinse dafly
Cribs
Filters and
rinse dafly
Cribs
Sample
Recovery
End of
series
End of
series
End of
series
End of
series
End of
series
End of
series
End of
series
End of
series
End of
series
End of
series
Dafly
Daily
WS\RD123.40
RJM1Z31A.RFT
3-19
-------
where it remained for the test series. (If the flow changes as
shown by the pitot the overall flow in the tunnel may be
changed based on the single point pitot reading).
The stack and tunnel were cleaned before the start of testing.
They were not cleaned again during this test program.
Method 5G
For all Crested Butte tests, each stove was tested using one Method 5G
sampling train, see Figure 3.14, for schematic of a ES single 5G train sampling in a
six inch vertical dilution tunnel.
The filters were changed at the end of each test day.
The probe and front filter bell were acetone rinsed at the end
of each test series.
The accumulative total of the filters weight gains plus the
acetone rinse weight gain were determined for the seven day
test period.
Due to the low percentage of the weight gain found in the acetone rinse, and
that the filters were recovered daily, the emission rates for cordwood based on the
filters only, were calculated on a daily basis. This provides more data points and a
greater certainty to the results.
The acetone rinse of the Method 5G sampling train was less than 3.1% of the
total weight gain for Test Series A-l and 2; B-l and 2: C-l, and 3 and less than 6.8%
for Test Series D-l, and 3.
Pitot and meter orifice readings were taken every 15 minutes.
Meter readings - Temperatures - so forth were taken at the
start and end plus hourly. (The stove surface temperature was
averaged.
VPI Test Method
One VPI train per stove.
Started and stopped each test day at the same time as the 5G
train.
The sample was recovered at the end of each test series.
The starting flow rate was ~8 milliliters per minute. To
provide "34 liters of sample in 70 hours.
VPI Sample Recovery
The sample recovery followed the same methods as outlined previously in
this section for the testing conducted at ES's RTP facility with the following
exceptions:
123.40
IA.RPT 3 - 20
-------
VPI Sampler
Probes were baked at 450 F for one hour and than dessicated
to constant weight before use.
Probe - The probe interior was rinsed and brushed with
acetone into the condensate sample.
Probe was then nitrogen purged for ~*/i hour at ".5 liter/per
minute.
The probe was than dessicated to a constant weight.
1/8" Teflon probe line: The line was flushed - three times
(visually clean) using 20 milliliters of acetone each time into
the condensate beaker, the line was not weighed.
The stainless steel tube between the condensate and filter was
rinsed with acetone into the condensate, the connector was not
weighed.
VPI Sample Calculations
The same computer program, VPI's as corrected 11-28-89, was used for both
the RTP and Crested Butte tests.
Mock Certification Test Procedures at Crested Butte for the Sweet Home AK-18
and the Country Comfort CC-150.
One test run was attempted in each burn rate category for a
total of 4 tests.
The stove burned Douglas Fir wood cribs during these tests.
The wood % moisture was determined by the standard
method.
The VPI sample rate was set at 60 milliliters per minute The
test ended when the coal bed was the same weight as it was at
the start of the test.
(After 10 hours of testing the primary air will be fully opened
to finish burning the wood if any is left).
The Method 5G and VPI train will be recovered before
starting the next test.
123.40
1ARPT 3-21
-------
SECTION 4.0
-------
SECTION 4
WOOD STOVE SPECIFIC INFORMATION
A total of 4 woodstoves were used for this test program.
The specific stoves used were:
Sweet Home AK-18 SN 0662
Country Comfort CC-150 SN 750-4865CC
Haugh's S-173E SN 792570
Ashley Oval SN (Unknown)
The AK-18 and CC-150 were used during both sections of the test program.
The S-173E and Ashley were used only at Crested Butte. The Ashley was provided
by arrangements through the Wood Heating Alliance. It was delivered and picked
up at the end of testing, by the wood stove retailer in Crested Butte.
Sweet Home AK-18 SN 0662
This is the AK-18 that was used for the 1988 EPA Wood Heater Testing
Laboratory Accreditation round robin test program. It was also used for the 1988
effects of elevation study at Mt. Mitchell, North Carolina. Figure 4.1 depicts the
modified stove (as used for all the studies) and shows representative gas flows.
Table 4-1 and 4-2 provide details of the stove. Table 4-1 is a description of
the stove as tested, and Table 4-2 describes the stove in its pre-modification
configuration. One additional change is the replacement of the combustion control
mechanism which was changed to a sealed system incorporating a 2-inch ball valve
for primary combustion air control.
The fire box volume of this stove is 2.0 cubic feet. The catalyst was provided
in the stove and is identified as the catalyst that was aged and used for baseline
testing, the 1988 inter-laboratory proficiency tests, and the Mt. Mitchell tests.
Country Comfort CC-150 SN 750-4865CC
This is the highly modified CC-150 used for the 1989 EPA Wood Heater
Testing Laboratory Accreditation round-robin test program and the 1988 special
study on the effects of elevation at Mt Mitchell, North Carolina.
Figure 4.2 shows the modifications of this stove. Figure 4.3 shows the
representative gas flows for this modified stove. The fire box volume of this stove is
1.52 cubic feet.
4-1
-------
Primary Combustion Air
Combustion Exhaust Gas
Slack
By-pass
Figure 4.1 Modified Sweet Home Model AK-18 Showing Gas Flows
4-2
-------
Table 4-1
MODIFIED SWEET HOME AK-18 DESCRIPTION
APPLIANCE IDENTIFICATION
Appliance manufacturer: Sweet Home Stove Works - Modified for EPA
Model: AK-18 (modified)
Type : Catalytic, freestanding
WOOD HEATER DESCRIPTION:
Materials of Construction: Welded steel plate body; cast iron
door, catalyst housing, and mixing plate.
Air Introduction System: Modified. Ball valve to airwash.
Combustion Control Mechanisms: Ball valve controlling primary air.
Combustor: Corning, 6" diameter, 25 cells/in.2. Supplied by EPA.
Internal Baffles: Horizontal baffle upstream of mixing plate.
Vertical baffle downstream of combustor.
Other Features: Mixing plate upstream of combustor.
Flue Outlet: 6" diameter, in rear of top surface of stove.
WOOD HEATER OPERATING INSTRUCTIONS
Specific written instructions.
4-3
-------
• P.O. Box 233 Sweet Home, OR 9738S
,,.„«,„„ pnon.numa., .Mr^-Iil
Name me; Modal nvrnia«r
Catalytic Fir MIC-18
AK 0652
Inaart .
i-0..ertpllon:(.
(503) 3S7-518S
Fi'rgoroof metal - fi'rgbox Ti'npd with
ntfcrfuc^an 5y3(»m : Air CCfngS in tn ^tp
able opening on bottom of stove - travels up sices of
fi'reoox (outsi'a'el and enters firebox at too ffmnH
"washes" down faca of door.
^uaticrt Cjn'-rcl Macnaniarr^l : On*3 h^nrfla ^Sj^ rpn^vn I <• ^ 1-? Xo
door aver air iniet apam'nc
inumai2s/:i4a: Sloooina baffle in front iust bpTnw
plate be lav/ catalyst on roof of firsbox.
fi'reoox below the catalyst
PlnwJacntf «
3«<1Jt .NlMTIfi
>1«
Corning
Model 6000
6" Ofa. 2" hfoh
..
12.6-15.4
16.5
„, Cor Better
19-25 _J;]
(16-20)
2.00
19.75
c/ Photograph o/T«al fu-I
Table 4.2 Description of AK-18 Before Modification
4-4
-------
o>
•&.
to
GO
r>
tr
a
0
O
ft.
g
EL
n
9
H-1
U»
O
d
n>
MODIFICATIONS
<^3
CUD
H-Tua'Xi u u u u a~u
In hn n n n n n n\
d
OQ
O
O
&.
O
BEFORE
LEGEND
AFTER
Plate welded to separate the firebox and secondary air channel
Insulation removed.
Steel strip over the back firebrick.
Secondary air hole.
Baffle removed-firebrick retaining tabs added.
Front welded.
-------
Primary Combustion Air
Secondary Combustion Air Psgmp^
Combustion Exhaust Gas
A A
Figure 4.3 Modified CC-150 Representative Gas Flows
4-6
-------
Haugh's S-173E SN 792570
This Haughes Model S-173E was prepared and baseline tested for the 1990
EPA Wood Heater Testing Laboratory Accreditation round-robin test program.
Figure 4.4 shows the S-173E as modified and representative gas flows. The fire box
volume is 1.498 cubic feet.
Description of the S-173E
Primary air enters the unit through two 1/2"H x 2" oval openings and is
naturally drafted through circular holes (two 1/2" and one 3/8" diameter) located in
the top front of the firebox. Air entering the holes is directed into the firebox by the
air deflector. Air entering the ovals are channeled to the right and left hand sides of
the air deflector and directed downward washing the door as it enters the firebox.
The primary air intake is regulated by a sliding control plate which traverses a
horizontal axis. The control plate movement is restricted by a 1/2" square stop,
located on the left side of the stove front. This stop is positioned to incorporate a
1/8" gap when in the fully closed position. At full open, the plate is slid far right.
All fires should be started in the open position.
The secondary air enters the stove at the bottom rear, and is routed vertically
through an air channel entering the secondary baffle. Air exits the secondary baffle
and enters the firebox through a series of 3/8" and 1/4" diameter holes. Primary air
and secondary air mix within the firebox and exhaust gases are exited through the
flue collar.
Ashley Oval SN Unknown
The Ashley Oval stove was provided by arrangements through the Wood Heater
Alliance. The Ashley was provided as a typical low tech wood heater as used in the
Crested Butte area prior to the 1989-1990 hearing season.
Description of Ashley Oval as Tested
The Ashley had both a top loading door and a front loading door. The front
door had a thermostat. However, adjusting the thermostat did not appear to affect
how the stove operated. The bum rate could not be controlled. The stove stack
opened directly into the firebox at the top rear of the firebox.
4-7
-------
SECONDARY
AIR INTAKE
PRIMARY AIR INTAKE
EXHAUST
PRIMARY AIR —
INSULATION, FIRE BRICK
AND STOVE DOOR ARE NOT
SHOWN FOR CLARITY
Figure 4.4 Haugh's S-173E With Representative Gas Flows
4-8
-------
APPENDIX A
VPI METHOD SAMPLER OPERATION AND PROCEDURES
'WS\RD123.40
RJM1231A.RPT
-------
OPERATING PROCEDURES FOR THE VPI SAMPLER
SAMPLER SETUP IN THE LABORATORY
Evacuate sampler to about 2 torr
Renew the dessicant (Gas -from filter set -flows up through the Drierite) •
Weigh -filters, connector tube, probe, and line. (Use anti-static device)
Assemble -filter set, line, and probe
-------
Loosen 1/B" Swagelok nut and pull back sample line slightly i -f .it (end of
line) is submerged
Start M2 flow at probe tip (0.5 1pm)
Disassemble -filter set, get wet weights of -filters and connectors
Wipe off exterior of connector with acetone
Filters and connector tube into dessicator
A-fter N2 -flows 10 minutes, disconnect line from probe union
Scrape and clean outside o-f probe
-------
IM-SITU TESTING DATASHEET
DATE DEPLOYED PRETEST SAMPLFLO wet ml per s
DATE RETRIEVED POST TEST wet ml per s
INITIAL HOURMETER FINAL HOURMETER
TEST LOCATION APPLIANCE :
SAMPLER SERIAL NUMBER SAMPLER SETPOINT ; DEG. C
PRETEST LEAK CHK: VAC= " H2O, " MANOM FELL " IN MINUTE
POSTTEST LEAK CHK: VAC= " H20, " MANOM FELL " IN MINUTE
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST + MIN. + MIN. +. MIN. + MIN. DELTA
PROBE+FITTING
SAMPLE LINE .
INITIAL
WEIGHING 24-36 HR.
DATE
TIME _
FILTER #1
FILTER #2
CONNECTOR
DATE
TIME
WASH PETRI
PRE-TEST: TANK VACUUM = _____ " Hg (P = ______ Torr absolute)
POST-TEST: TANK VACUUM = _____ " Hg (P = ______ Torr absolute at T = ___ C)
WOOD SPECIES _____________________________ • _______ POST-TEST GAS ANALYSIS
WOODPILE: _______ Initial ________ Final wet Ib _______ 7.C02
WOOD MOISTURE CONTENT ________ dry 7. _______ '/.CO
A - 3
-------
10 .CLS'sampler, has 19890918 1134 (-from insitu.col 19890504 0329)
20 PRINT'THIS PROGRAM ASSUMES THE C02 ANALYZER 13 ZEROED ON ROOM AIR."
30 XC=.51:PRINT ' MASS FRACTION OF CARBON IN DRY WOOD
4O VOLUHE=.0736'TANK VOLUME IN CUBIC METERS
50 INPUT "TANK TEMPERATURE IN CELCIUS WHEN FINAL PRESSURE MEASURED" ; T:T=27J,ij
60 INPUT "DRY 7. C02":C02
70 INPUT "DRY 7. CO"; CO
80 INPUT "DRY 7. 02 (ENTER 0 IF UNKNOWN)"; 02
90 INPUT "TOTAL CATCH (GRAMS)";CATCH
100 INPUT "WET WOOD BURNED (kg)";WETWOOD
110 INPUT "DURATION OF TEST IN HOURS";HOURS
120 INPUT "WOOD MOISTURE CONTENT (DRY 7.) "; MCDRY: MCDRY=MCDRY/100
130 INPUT "TANK ABSOLUTE PRESSURE BEFORE SAMPLING (TORR)";TORR1
140 INPUT "TANK ABSOLUTE PRESSURE AFTER SAMPLING (TORR)";TORR2
150 IF 02<. 000001 THEN 02=21-C02-CO/2' ESTIMATE 02 DRY 7. FROM C02 AND CO
160 N2=100-C02-CO-02' NITROGEN (DRY 7.1
170 M=(44*C02+28*CO+32*02+2S*N2)/100' MOLECULAR WEIGHT, 6/GMOL
ISO AF=N2*4. 76/3. 76*297 (12* (C02+1.5*CO) )*XC' DRY A/F RATIO ASSUMING C02 ANALY!
IS ZEROED ON ROOM AIR
190 PRINT "AIR-FUEL RATIO = ";:PRINT USING "###.#".;AF
200 RHO=(TORR2-TORR1)7760*101.325/a.314*M/T'kg/m^3-DENSITY OF POST-TEST TANKl
210 SAMPLEFLOW=RHO*VOLUME/HOURS' dry sample -flow,ka/hr
220 STACKFLOW=(AF+1)/HOURS*WETWOOD*<1/( H-MCDRY)) ' DRY STACK FLOW, kg/hr
230 SMOKEGHR=CATCH*STACKFLOW/SAMPLEFLOW/HOURS
235 PRINT
240 PRINT "SMOKE = ";:PRINT USING "###. tt" ; SMOKEGHR; : PRINT " jj
245 BRATE=WETWOOD*(I/(1+MCDRY) )/HOURS' DRY KG/HR
250 PRINT "WOOD BURN RATE = "jsPRINT USING "tttttt.#";BRATE;:PRINT " dryj
hr "
255 SFLOWGS=STACKFLOW*1000/3600' dry g/s
260 PRINT "STACK FLOW = "; -PRINT USING "tt##. ft" ; SFLOWGS; :PRINT " dry
/s"
270 COGHR=STACKFLOW/M*CO/100*28*1000
275 PRINT "CO = ";:PRINT USING "####. ft" ; COGHR; -PRINT " g/hr
230 COGKG=COGHR/BRATE
285 PRINT "CO = ";s PRINT USING "###. tt" ; COGKG; : PRINT " g/kg
290 SMOKEGKG=SMOKEGHR/BRATE
295 PRINT "SMOKE = ";: PRINT USING "###. ft" ; SMOKEBKG; : PRINT " g/
A - 4
-------
APPENDIX B
EQUIPMENT QA/QC AND CALIBRATION
\RD123.40
W231A.RFT
-------
METHOD 5-G - EQUIPMENT CALIBRATION SUMMARY
Equipment
Calibration
Frequency
Date
Pitot (standard type)
Manometers
Thermocouples
Barometer (Mercury)
Barometer (Aneroid)
Dry Gas Calibration
Meter #6845706
Dry Gas Meter #6846746
Dry Gas Meter #717454
Dry Gas Meter Rac-D
Analytical Balance
Top Loader Balance
Visual when new
Visual before test
From the factory
Before use checked
to and against ambient
From the factory
Semi annually
Annually
Pre and Post Test
Series
Pre and Post Test
Series
Semi-annually
before each use
Before each use
Daily
NA
Daily
NA
5/5/89
5/8-9-89
See attached
Data Sheets
For actual
calibrations
Daily
Daily
VPI METHOD-EQUIPMENT CALIBRATION SUMMARY
Equipment
Low Flow Rotometer
Medium Flow Rotometer
Calibration
Frequency
Date
Before use
Before use
11/8/89
10/13/89
B-l
-------
METHOD 28
EQUIPMENT CALIBRATION SUMMARY
Equipment
Platform Scale and
Monitor (10 Ibs)
Scale Calibration
Weights
Draft Gauge
Anemometer
Barometer (Mercury)
Barometer (Aneroid)
Thermometers
(Calibration)
Humidity Gauge
(Sling Psychrometer)
Thermocouples
Wood Moisture Meter
Wood
Dilution Tunnels
Cleaned RTP Dilution
Dilution Tunnels
/Tf _. J X"*( i J T^ i i _
Calibration
Frequency
Beginning and end of
Once
Never (from the
factory)
Once
Never (from the
factory)
Semiannually
Never (from the
factory)
Once
Ambient before use
Before each use
When purchased
(Green Douglas Fir
"C" grade or better)
Before test series
Before test series
Date
Calibrated
Daily
2/18/88
N/A
2/18/88
N/A
5/5/89
N/A
3/9/88
Daily
Daily
9/16-17/89
New Pipe
B-2
-------
Sweet Home AK-18
Train A
Meter Box #ES-3
Train B
Meter Box #AES-1
APPENDIX B
Meter Box Calibration Summary
Test Phase 1RTP North Carolina
Pre Test
9/16/89 (1.007)
8/29/89 (1.029)
Country Comfort CC-150
Train A
Meter Box #Nutech A
Train B
Meter Box #Nutech B
8/17/89 (0.995)
8/17/89 (1.009)
Post Test
10/10/89 (1.039)
10/10/89 (1.036)
10/11/89 (0.996)
10/11/89 (1.019)
VPI Rotometer 10/13/89 Used RTP North Carolina
Setting
70
68
65
64
mL/min
66.7
60.6
57.8
57.1
Setting
62
61
60
mL/min
56.8
54.6
51.7
B-3
-------
Test Phase 2 Crested Butte, Colorado
Country Comfort-CC-150
Train A
Meter Box Nutech "A"
Pre Test
8/17/89 (0.995)
Sweet Home AK-18
Train B
Meter Box Nutech "B"
8/17/89 (1.009)
Haughes S-173E
Train C
Meter Box EPA 037597
(1.046)
Ashley Oval
Train D
Meter Box Rac "D"
(0.974)
Rotometers for VPI used Crested Butte, Colorado
Post Test
Test Series^ 1 (1.001)
Test Series #2
11/20/89 (1.000)
Test Series #3
12/3/89 (0.982)
Test Series #1
11/14/89 (1.014)
Test Series #2
11/20/89 (1.003)
Test Series #3
12/5/89 (0.989)
Test Series #1
11/14/89 (1.029)
Test Series #2
11/20/89 (1.046)
Test Series #3
12/4/89 (1.049)
Test Series #1
11/14/89 (0.971)
Test Series #2
11/20/89 (1.046)
Test Series #3
12/3/89 (0.964)
Low Flow
Setting
11-8-89
75
73
12-4-89
74
71
65
60
TnT./min
Actual
8.2
7.7
8.5
7.9
7.5
6.9
mL/min
Standard
6.2
5.8
6.1
5.7
5.4
5.0
Medium Flow
Setting
11-8-89
69
12-4-89
69
62
59
54
50
mL/min
Actual
61.0
57.8
52.6
49.0
45.4
41.9
mL/min
Standard
45.9
41.7
37.9
35.3
32.7
30.2
S\RD 123.40
JM1231A.RPT
B-4
-------
orr «AS arrw
DATA
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tafc cn«ek front
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-------
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B - 6
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-------
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-------
APPENDIX C
VPI GAS ANALYSIS RESULTS
WS\RD123.40
RJM1381AAPP
-------
TEST NO.
%CO2
ESLAB
UPI TANK ANALYSIS
%CO/
TOTAL
SH-1A
SH-1B
SH-2A
SH-2B
SH-3A
SH-3B
SH-4A
SH-4B
SH-5A
SH-5B
SH-6A
SH-6B
SH-7A
SH-7B
SH-8A
SH-8B
TEST NO.
CCS-lAd
CCS-1B
CCS-2A
CCS-2B
CCS-3A
CCS-3B
CCS-4A
CCS-4B
CCS-5A
CCS-5B
CCS-6A
CCS-6B
CCS-7A
CCS-7B
CCS-8A
CCS-8B
0.20
0.23
0.47
0.45
3.93
3.91
0.56
0.54
0.34
0.34
0.20
0.21
0.15
0.15
0.10
0.11
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0.92
1.28
0.67
0.64
1.21
1.18
1.04
1.01
1.81
1.83
2.71
2.71
1.87
1.87
0.84
0.83
12.34
12.34
14.44
14.74
8.74
8.64
14.24
14.04
14.24
14.40
14.64
14.64
15.32
15.40
15.27
15.27
%CO^
5.25
7.15
8.94
8.94
8.94
8.74
9.34
9.24
7.65
7.65
5.05
5.05
7.04
6.95
9.14
9.14
7.87
8.00
5.62
5.24
10.00
10.00
5.99
624
6.19
5.99
5.69
5.74
5.12
4.99
4.99
5.02
%0A
15.25
13.13
11.50
11.38
11.00
11.13
10.88
11.13
11.75
11.75
14.38
14.46
12.75
12.95
11.08
11.20
20.4
20.6
20.53
20.4
22.7
22.6
20.8
20.8
20.8
20.7
20.5
20.6
20.5
20.5
20.4
20.4
TOTAL
21.4
21.6
21.1
21.0
21.2
21.0
21.3
21.4
21.2
21.2
22.1
22.2
21.7
21.8
21.1
21.2
C - 1
-------
a. CO Calibration Curve Y = (0.0491)(X) + 0.0558 except for SH-2A, SH-2B,
CCS-5A and CCS-5B when it is Y = (0.0495)(X) + 0.0764
b. CO2 Calibration Curve Y = (0.1990)(X) + 0.0499
c. O2 CaHbration Curve Y = (0.2504)(X)-0.0161
d. Small leak in the sample system
c - 2
-------
CRESTED BUTTE
UPI TANK ANALYSIS
STOVE TEST %COa %CO2b %02C TOTAL
A Series #ld 1.81 8.41 11.50 21.7
A Series #2 1.34 6.68 13.50 21.5
A Mock Cert. 3-1 2.46 6.68 13.12 22.3
A Mock Cert. 3-2 1.46 9.88 10.25 21.6
A Mock Cert. 3-3 1.51 9.32 10.50 21.3
A Mock Cert. 3-4 1.59 10.08 10.00 21.7
B Series #ld 1.09 13.50 6.38 21.0
B Series #2 0.86 12.48 7.63 21.0
B Mock Cert. 3-1 0.19 13.07 7.26 20.5
B Mock Cert. 3-2 0.16 9.88 10.75 20.8
B Mock Cert. 3-3 0.21 13.28 7.26 20.8
B Mock Cert. 3-4 0.36 13.78 6.88 21.0
C Series #ld 1.21 9.09 11.00 21.3
Ce Series #2 0.46 3.08 17.50 21.0
C Series #3 1.14 8.68 11.63 21.4
D Series #ld 0.30 4.78 15.50 20.6
D Series #2 0.59 4.88 15.62 21.1
D Series #3 0.64 4.68 16.00 21.3
a. For Test Series 1 Calibration Curve is Y = (0.0481)(X) + 0.1296
b. For Test Series 1 Calibration Curve is Y = (001959)(X) + 0.0837
c. Calibration Curve is Y = (0.2497)(X) + 0.0161
d. After Test Series #1 the CO/CO2 Analyzer was replaced
e. The train leaked at the end of the test series due to a cracked filter holder
c - 3
-------
APPENDIX D
SAMPLE BLANKS
S\KD123.40
M1381AAPP
-------
PARTICULATE WEIGHT SUMMARY
FILTER AND BEAKER BLANKS
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-------
APPENDIX E
GRAPH VALUES AND FORMULAS
*Note: 0 as shown in the Tables are for the computer graphing program
WS\RD123.40
WM1381AAPP
-------
VPI METHOD VERUS EPA METHODS 28/5G
RUN*
SH-U
SH-1B
SH-2A
SH-2B
SH-3A
SH-3B
SH-4A
SH-4B
SH-5A
SH-5B
SH-6A
SX-6B
SH-7A
SH-7B
SH-8A
SH-8B
CC5-1A
CCS- 18
CCS-2A
CC5-2B
CCS-3A
CCS-3B
CCS-4A
CC5-48
CCS-SA
CCS-5B
CC5-6A
CCS-6B
CCS-7A
CCS -78
CC5-8A
CCS -88
A- 1 -TOTAL
A- 2- TOTAL
A-3-1
A-3-2
A-3-3
A-3-4
A-3-SUH
B-1-SUM
•-2-SUM
S-3-1
B-3-2
S-3-3
8-3-4
B-3-TOTAL
C-1-SUM
C-2-SUH
C-3-SUM
D-1-SUM
VPI
(ACT)
3.100
3.300
1.000
1.000
16.400
16.100
2.900
2.200
1.600
2.600
2.300
2.700
1.900
1.700
1.700
1.200
22.500
23.300
9.400
8.900
17.700
20.200
13.300 .
12.400
29.300
30.700
21.200
20.600
23.300
24.200
6.600
6.800
31.300
30.400
38.800
16.300
24.700
23.100
25.700
10.900
16.600
0.900
2.900
3.800
3.200
2.700
20.800
25.400
16.600
38.500
5G
(ACT)
1.42
1.46
0.59
0.60
13.53
13.93
1.97
1.93
1.38
1.39
1.32
1.24
1.14
1.13
0.79
0.95
14.92
14.78
7.45
7.53
13.78
13.90
8.67
8.90
22.69
22.82
15.68
15.98
15.77
15.13
5.50
5.52
18.84
20.97
27.87
11.48
15.14
16.76
17.80
7.05
10.14
0.65
1.37
1.76
1.67
1.37
12.23
12.27
11.87
26.64
5C
(ADJ)
2.440
2.490
1.170
1.190
15.810
16.200
3.190
3.140
2.380
2.390
2.290
2.170
2.020
2.010
1.500
1.740
17.160
17.020
9.640
9.720
16.060
16.-170
10.930
11.170
24.290
24.410
17.870
18.150
17.950
17.360
7.500
7.310
20.820
22.750
28.830
13.800
17.360
18.890
19.860
9.200
12.450
1.280
2.370
2.910
2.790
2.370
14.540
14.580-
14.180
27.750
VPI(ACT) CCWVEXSIOM TO SG(ACT)
EASED OH ALL VPI RUNS
Regression Output:
Constant -0.261
Std Err of T Est ' 1.466
« Squired 0.973
Xo. of Observations 52.000
Degrees of Freedom 50.000
X Coefffeient(s)
Std Err of Coef.
0.712
0.017
5G=(.71ZXVPI ACT)-.216
YPJ(ACT) COMVERSIOM TO 5CCADJ)
BASED ON ALL VPI RUMS
Regression Output:
Constant 1.094
Std Err of T Est 1.477
R Squared 0.974
Xo. of Observations 52.000
Degrees of Freedom 50.000
X Coeffieient(s)
Std Err of Coef.
0.728
0.017
5GCAOJ>(.728)(VPI ACT)*1.094
.•Data 'for Figure 1". 1 aiul '2.1
E - 1
-------
VPI CARBON MONOXIDE COMPARISON ES UOCOSTOVE US vs CRESTED BUTTE
VPI CARBON MONOXIDE SUM/HOUR
RUN * BURN RATE AC-18 AIMS CC150 CE150
kg/hr LAS C B US C B
SH-1A
SH-IB
SH-2A
SH-3 SH-2B
OUTLIER SH-4A
HOT USED SH-4B
SH-5A
SH-5B
SH-6A
SH-68
SH-7A
SH-78
SH-8A
SH-8B
8-3-1
8-3-2
8-3-3
8-3-4
8-3-SUH
CC5-1A
CC5-1B
CC5-2A
CC5-2B
CC5-3A
CC5-38
CC5-4A
CCS-4B
CC5-5A
CC5-5B
CC5-6A
CC5-6B
CCS-7A
CCS-78
CC5-8A
CC5-88
A-3-1
A-3-2
A-3-3
A-3-4
A-3-SUH
1.560
1.560
0.740
0.740
1.810
1.810
1.880
1.880
1.330
1.330
1.140
1.140
1.040
1.040
0.660
1.100
1.150
1.320
1.060
1.170
1.170
1.860
1.860
1.390
1.390
1.490
1.490
0.780
0.780
0.450
0.450
0.820
0.820
1.680
1.680
0.700
1.060
1.200
1.270
1.060
20.900
34.100
27.800
26.200
80.900
77.100
52.100
51.500
21.400
22.500
13.400
13.200
8.100
8.900
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
o.ooo
0.000
0.000
0.000
o.ooo
o.ooo
0.000
0.000
0.000
o.ooo
o.ooo
0.000
0.000
o.ooo
0.000
0.000
o.ooo
o.ooo
o.ooo
6,000
0.000
0.000
0.000
o.ooo
0.000
0.000
0.000
o.ooo
0.000
a. ooo
11.300
20.800
21.400
39.800
23.300
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
o.ooo
0.000
0,000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
194.200
197.700
150.600
144.800
188.400
188.200
170.400
167.400
163.900
165.200
163.000
162.900
187.500
189.000
163.100
161.100
0.000
0.000
0.000
o.ooo
0.000
0.000
0.000
> 0.000
0.000
0.000
0.000
0,000
0.000
o.'ooo
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
o.ooo
o.ooo
0.000
0.000
0.000
0.000
o.ooo
0.000
0.000
0.000
0.000
0.000
O.GOO
0.000
0.000
200.900
153.700
188.200
195.300
184.500
AK-18 CO LAB
Regression Output:
Constant
Std Err of Y Est
t Squared
No. of Observations
Degrees of Freedom
X Coeffieient(s) 43.90018
Std Err of Coef. 11.83485
AK-18 CO CRESTED BUTTE
Regression Output:
Constant
Std Err of Y Est
tt Squared
Xo. af Observations
Degrees of Freedom
X Coefficient(s) 37.16790
Std Err of Coef. 11.75229
CC-150 CO LAB
Regression Output:
Constant
Std Err af Y Est
R Squared
Mo. of Observations
Degrees of Freedom
X Coefficients) -9.32972
Std Err sf Coef. 8.794006
CC-150 CO CRESTED BUTTE
Regression Output:
Constant
Std 'Err of Y Est
It Squared
He. ef Observations
Degrees af Freedom
-26.7145
17.14169
0.534154
14
12
-16.0036
5.724707
0.769267
5
3
183.5798
16.07259
0.074413
16
14
201.5865
20.79771
0.037311
5
3
• X Coefficients) -16.1310
. -Std Err of Coef. 47.30664
Data/for Figure'1.2 -and 2.2'
E - 2
-------
AK-18 METHOD 5G/28
RUN #
DUMMY
DUMMY
SH-1A
SH-1B
SH-2A
SH-4A
SH-4B
SH-5A
SH-5B
SH-6A
SH-6B
SH-7A
SH-7B
SH-8A
SH-88-.
B-3-1
B-3-2
B-3-3
B-3-4
MM
MM
MM
MM
MM
MM
MM
HH
BURN RATE
0.250
2.SOO
1.56
1.56
0.74
1.81
1.81
1.88
1.88
1.33
.33
.14
.14
.04
.04
0.66
1.10
1.15
1.32
0.470
0.500
0.830
0.920
1.280
1.430
1.440
1.450
LAB
0.000
0.000
2.44
2.49
1.17
3.19
3.14
2.38
2.39
2.29
2.17
2.02
2.01
1.50
1.74
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
LAB C
DUMMY B
0.693
3.681
2.433
2.433
1.344
2.765
2.765
2.858
2.858
2.127
2.127
.875
.875
.742
.742
.237
.822
1.888
2.114
0.985
1.025
1.463
1.583
2.061
2.260
2.273
2.287
RESTED
UTTE
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.28
2.37
2.91
2.79
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
C B
DUMMY H
0.318
5.943
3.593
3.593
1.543
4.218
4.218
4.393
4.393
3.018
3.018
2.543
2.543
2.293
2.293
1.343
2.443
2.568
2.993
0.868
0.943
1.768
1.993
2.893
3.268
3.293
3.318
HOOT
ITCHELL
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.740
1.380
2.400
3.140
3.170
2.620
2.320
2.940
X H
DUMMY
1.361 AK-18 ES LAB
4.326 Regression Output:
3.087 Constant
3.087 Std Err of Y Est
2.006 R Squared
3.417 Mo. of Observations
3.417 Degrees of Freedom
3.509
3.509 X Coefficient(s) 1.328
2.784 Std Err of Coef. 0.224
2.784
2.534 AK-18 CRESTED BUTTE
2.534 Regression Output:
2.402 Constant
2.402 Std Err of Y Est
1.901 R Squared
2.481 Ho. of Observations
2.547 Degrees of Freedom
2.771
1.650 X Coefficient(s) 2.500
1.690 Std Err of Coef. 0.596
2.125
2.244
2.718
2.916 AK-18 HOUHT MITCHELL
2.929 Regression Output:
2.942 Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of Freedom
X Coefficient(s) 1.318
Std Err of Coef . 0.575
0.361
0.291
0.762
13.000
11.000
-0.307
0.290
0.898
4.000
2.000
1.031
0.633
0.467
8.000
6.000
Data for Figure 2.3
-------
CC-150 METHOD 5G/28
RUN e
BURN RATE
LAS
LAB CRESTED
DUMMY .BUTTE
DUMMY
DUMMY
CC5-1A
CCS- IB
CCS-2A
CCS -28
CCS-3A
CCS-3B
CCS-4A
CCS-4B
CCS-5A
CCS-SB
CCS-6A
CCS-6B
CCS-7A
CCS-7B
CC5-8A
CC5-8B
A-3-1
A-3-2
A-3-3
A-3-4
MM
MM
MM
MM
MM
MM
m
MM
1.000
2.000
1.17
1.17
1.86
1.36
1.39
1.39
1.49
1.49
0.78
0.78
0.4S
0.45
0.82
0.82
1.68
1.68
0.70
1.06
1.20
1.27
0.550
0.740
0.810
0.340
1.330
1.440
1.550
1.570
0.000
0.000
17.16
17.02
9.64
9.72
16.06
16.17
10,93
11.17
24.29
24.41
17.87
18.15
17.95
17.36
7.50
7.51
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
17.061
7
.897
15.503
15.503
9.180
9.180
13.487
13.
12.
,487
,571
12.571
19,
,077
19.077
22.101
22.101
18.711
18.711
10.829
10.829
19.
16.
15.
14.
21.
19.
18.
18.
14.
13.
12.
11.
810
511
223
587
185
444
802
527
037
029
021
838
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
28.83
13; 80
17.36
13.89
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
C B
MOOT
DUMMY HITCHELL
20.844
1.265
17.516
17.516
4.006
4.006
13.208
13.208
11.250
11.250
25.151
25.151
31.612
31.612
24.368
24.368
7.530
7.530
26.718
19.669
16.928
15.558
29.655
25.935
24.564
23.977
14.383
12.229
10.076
9.684
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
22.760
16.300
23.320
21.170
12.460
9.600
10.830
10.640
K H
DUMMY
17.220
4.354
15.033
15.033
6.155
6.155
12.202
12.202
10.916
10.916
20.051
20.051
24.296
24.296
19.536
19.536
8.471
8.471
21.080
16.448
14.647
13.746
23.010
20.565
19.665
19.279
12.974
11.559
10.144
9.886
CC150 ES LAB
Regression Output:
Constant
Std Err of Y Est
R Squared
Ho, of Observations
Degrees of Freedom
X Coefficient(s) -9,164
Std Err of Coef. 1.715
CC150 CRESTED BUTTE
Regression Output:
Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of freedom
X Coefficient(s) -19.579
Std Err of Coef. 11.393
CC150 MOUNT HITCHELL
Regression Output:
Constant
Std Err of T Est
R Squared
Mo. of Observations
Degrees of Freedom
X Coefficient(s) -12.866
Std Err of Coef. 2.391
26
3
0
16
14
40
5
0
4
2
.225
.134
.671
.000
.000
.423
.009
.596
.000
.000
30.086
2.593
0.828
8,
6.
,000
.000
Data for Figure 2.4
E - 4
-------
SWEET HOME AK-18 CORDUOOD vs 5G(AOJ)/METHCO 28
RUN* BURN RATE 5G ACT SGasSH
kg/hr g/hr g/hr
LAB
CB COROUOOO
CB 5G(ADJ)
DUMMY
DUMMY
SH-1A
SH-1B
SH-2A .
SH-2B
SH-4A
SH-4B
SR-5A
SH-58
SH-6A
SH-6B
SH-7A
SH-78
SH-8A
SH-83
B-1-1
B-1-2
B-1-3
8-1-4
B-1-5
B-1-6
B-1-SUM
B-2-1
B-2-2
B-2-3
B^ /
•Z-H
B^ e
•Z-5
B-2-6
B-2-SUH
B-3-1
B-3-2
B-3-3
B-3-4
B-3-TOTAL
0.300
2.500
1.56-
1.56
0.74
0.74
1.81
1.81
1.88
1.88
1.33
1.33
1.14
1.14
1.04
1.04
1.03
0.76
0.78
0.72
0.55
0.89
0.79
1.02
0.96
1.15
0*»/
.OH
0.95
1.00
0.99
0.66
1.10
1.15
1.32
1.06
1.42 .
1.46
0.59
0.60
1.97
1.93
1.38
1.39
1.32
1.24
1.14
1.13
0.79
0.95
10.84
5.56
6.94
4.50
2.01
11.22
7.05
5.84
11.09
18.61
3.93
10.86
5.24
10.14
0.65
1.37
1.76
1.67
1.37
0.000
0.000
2.44
2.49
1.17
1.19
3.19
3.14
2.38
2.39
2.29
2.17
2.02
2.01
1.50
1.74
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.701
3.722
2.431
2.431
1.305
1.305
2.774
2.774
2.870
2.870
2.115
2.115
1.854
1.854
1.717
1.717
1.703
1.332
1.360
1.278
1.044
1.511
1.374
1.689
1.607
1.868
1.442
1.593
1.662
1.648
1.195
1.799
1.868
2.101
1.744
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
13.16
7.56
9.09
6.34
3.24
13.54
9.20.
7.88
13.41
20.60
5.67
13.17
7.20
12.45
0.000
0.000
0.000
0.000
0.000
-2.518
45.002
24.698
24.698
6.986
6.986
30.098
30.098
31.610
31.610
19.730
19.730
15.626
15.626
13.466
13.466
13.250
7.418
7.850
6.554
2.882
10.226
8.066
13.034
11.738
15.842
9.146
11.522
12.602
12.386
5.258
14.762
15.842
19.514
13.898
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.28
2.37
2.91
2.79
2.37
0.447
5.947
3.597
3.597
1.547
1.547
4.222
4.222
4.397
4.397
3.022
3.022
2.547
2.547
2.297
2.297
2.272
1.597
1.647
1.497
1.072
1.922
1.672
2.247
2.097
2.572
1.797
2.072'
2.197
2.172
1.347
2.447
2.572
2.997
2.347
LAB SG(ADJ) METHOD 28
Regression Output:
Constant
Std Err of Y Est
R Squared
Ho. of Observations
Degrees of Freedom
X Coeffici-enUs) 1.373
Std Err of Coef. 0.194
CRESTED BUTTE CORDUOOD
Regression Output:
Constant
Std Err of Y Est
R Squared
Mo. of Observations
Degrees of Freedom
X Coefficient(s) 21.600
Std Err of Coef. 5.348
CRESTED BUTTE 5G(ADJ) METHOD
Regression Output:
Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of Freedom
X Coefficient^) 2.500
Std Err of Coef. 0.487
0.289
0.281
0.807
14.000
12.000
-8.998
3.028
0.576
14.000
12.000
28
-0.303
0.237
0.898
5.000
3.000
Data for Figure 2.5
E - 5
-------
CC-150 CORDWOOO vs 5G(ADJ)/METHCO 28
RUM* BURM RATE 5G ACT SGasSH
kg/hr g/hr g/hr
LAS
CB CORDWOCO
CB 5GCADJ)
DUMMY
OUMMT
CCS-1A
CCS- IB
CCS-2A
CCS -28
CCS-3A
CCS-3B
CC5-4A
CC5-4B
CCS-5A
CC5-5B
CC5-6A
CCS -68
CC5-7A
CCS-7B
CCS-8A
ccs-as
A-1-1
A- 1-2
A-1-3
A-1-4
A-1-5
A-1-6
A-1-TOTAL
A-2-1
A-2-2
A-2-3
A^ c
•Z-5
A-2-6
A-2- TOTAL
A-3-1
A-3-2
A-3-3
A-3-4
A-3-SUM
0.300
2.500
1.17
1.17
1.86
1.86
1.39
1.39
1.49
1.49
0.78
0.78
0.45
0.45
0.82
0.82
1.68
1.68
0.93
0.75
0.56
0.46
0.72
0.84
0.71
0.83
0.63
0.72
0.94
1.04
0.87
0.70
.1.06
1.20
1.27
1.06
14.92
14.78
7.45
7.53
13.78
13.90
8.67
8.90
22.69
22.82
15.68
15.98
15.77
15.13
5.50
5.S2
17.21
20.86
20.14
13.04
24.87
14.63
18.84
22.23
14.72
20.66
19.66
16.06
20.97
27.89
11.48
15.14
16.76
17.80
0.000
0.000
17.16
17.02
9.64
9.72
16.06
16.17
10.93
11.17
24.29
24.41
17.87
18.15
17.95
17.36
7.50
7.51
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
23.476
3.315
15.S03
15.503
9.180
9.180
13.487
13.437
12.S71
12.571
19.077
19.077
22.101
22.101
18.711
18.711
10.829
10.329
17.702
19.352
21.093
22.010
19.627
18.527
19.719
18.161
20.452
19.627
17.611
16.694
18.252
19.810
16.511
15.228
14.587
16.511
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
"0.000
0.000
0.000
0.000
0.000
0.000
0.000
19.31
22. 6S
22.00
15.33
26.21
16.87
20.82
23.88
16.96
22.47
21.56
18.23
22.75
0.000
0.000
0.000
0.000
0.000
19.160
26.306
21.986
21.986
24.227
24.227
22.701
22.701
23.026
23.026
20.719
20.719
19.648
19.643
20.849
20.849
23.643
23.643
21.207
20.622
20.005
19.630
20.525
20.914
20.492
21.044.
20.232
20.525
21.239
21.564
21.012
20.460
21.629
22.084
22.311
21.629
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
28.83
13.80
17.36
18.89
19.86
34.586
17.5S4
17.554
4.046
4.046
13.247
13.247
11.289
11.
,289
CC150 5G
-------
HAUGHE'S S-173E METHOD 28 VERUS CORDWOOD
S-173E
RUNS
C-1-1
C-1-2
C-1-3
C-1-4
C-1-5
C-1-6
C-1-SUH
C-2-1
C-2-2
C-2-3
C-2-4
C-2-5
C-2-6
C-2-SUM
C-3-1
C-3-2
C-3-3
C-3-4
C-3-5
C-3-6
C-3-7
C-3-SUM
A-11
B-11
A-10
8-10
A-2
B-2
A-9
B-9
A-7
B-7
A-8
B-8
A-6
B-6
A-1
B-1
A-3
8-3
At
-4
8-4
A-5
BURN
RATE
1.06
1.09
0.97
0.86
0.85
0.79
. 0.94
1.03
0.80
1.14
1.13
0.87
0.78
0.97
1.34
1.09
1.43
0.98
1.17
0.92
0.98
1.13
0.620
0.620
0.710
0.710
1.110
1.110
1.140
1.140
1.160
1.160
1.210
1.210
1.320
1.320
1.420
1.420
1.560
1.560
2.860
2.860
3.050
CB
AS 5H
21.05
6.77
12.30
11.60
19.41
12.60
14.54
15.82
13.12
17.50
15.64
12.36
9.06
14.58
16.73
8.54
10.77
18.35
10.52
20.86
9.31
14.18
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
CB LINE
DAILY
13.880
13.870
13.910
13.946
13.950
13.969
13.920
13.890
13.966
13.854
13.857
13.943
13.973
13.910
13.788
13.870
13.758
13.907
13.844
13.926
13.907
13.857
14.025
14.025
13.996
13.996
13.864
13.864
13.854
13.854
13.847
13.847
13.831
13.831
13.794
13.794
13.761
13.761
13.715
13.715
13.286
13.286
13.224
LAB
5G(AOJ)
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
23.460
23.500
30.980
30.950
5.740
5.650
6.870
6.960
8.390
8.290
4.800
4.730
6.010
5.940
10.900
10.790
5.560
5.590
12.030
12.400
9.400
LABLINE
12.654
12.556
12.951
13.313
13.346
13.544
13..050
12.753
13.511
12.391
12.424
13.280
13.577
12.951
11.732
12.556
11.436
12.918
12.292
13.116
12.918
12.424
14.104
14.104
13.807
13.807
12.490
12.490
12.391
12.391
12.325
12.325
12.160
12.160
11.798
11.798
11.469
11.469
11.007
11.007
6.725
6.725
6.099
SUM
0.000
0.000
0.000
0.000
0.000
0.000
14.540
0.000
0.000
0.000
0.000
0.000
0.000
14.580
0.000
0.000
0.000
0.000
0.000
0.000
0.000
14.180
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
SUM LIKE
14.338
14.275
14.527
14.757
14.778
U.904
14.590
14.401
14.883
14.171
14.192
14.736
14.925
14.527
13.751
14.275
13.563
14.506
14.108
14.632
14.506
14.192
15.260
15.260
15.072
15.072
14.233
14.233
14.171
14.171
14.129
14.129
14.024
14.024
13.793
13.793
13.584
13.584
13.290
13.290
10.565
10.565
10.167
HAUGHS S-173E CRESTED BUTTE
Regression Output:
Constant
Std Err of T Est
R Squared
No. of Observations
Degrees of Freedom
X Coefficient(s) -0.330
Std Err of Coef. 5.279
HAUGHS S-173E CRESTED BUTTE
Regression Output:
Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of Freedom
X Coefficient(s) -2.096
Std Err of Coef. 0.509
HAUGHS S-173E BASELINE
Regression Output:
Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of Freedom
X Coefficient(s) -3.294
Std Err of Coef. 2.270
14.227
4.099
0.000
22.000
20.000
SUMS
16.557
0.074
0.944
3.000
1.000
16.146
7.971
0.095
22.000
20.000
Data for Figure 2.7
E - 7
-------
ASHLEY OVAL CORDWOOD DAILY AND 70 HOUR TESTS
RUN*'
EF25-EF20
Run Mo.:
0-1-1
0-1-2
0-1-3
0-1-4
0-1-5
0-1-6
D-1-SUH
D-2-1
0-2-2
0-2-3
0-2-4
0-2-5
D-2-6
D-2-SUM
0-3-1
0-3-2
0-3-3
0-3-4
0-3-5
0-3-6
0-3-7
D-3-SUM
OUHMY
DUMMY
BURN RATE
kg/hr
BURN 5
1.49
1.71
1.55
1.09
1.42
1.46
1.45
2.14
1.45
2.02
1.43
1.47
1.62
1.67
2.14
1.91
. 1.S2
0.97
1.91
1.02
1.65
1.64
0.200
3.000
5G ACT
S/hr
iG(ACT) 5
33.42
17.32
15.13
25. 68
43.07
20.28
26.64
20.85
26. S9
31.68
34.02
35.62
31.53
32.46
45.69
41.93
21.99
10.79
42.60
19.16
23.39
31.56
0.000
0.000
5G as 5
g/hr
iG(ADJ)
33.49
19:41
17.35
26.92
41.35
22.13
27.75
22.65
27.96
32.04
34.00
35.32
31.92
32.69
43.42
40.43
23.66
13.11
40.98
21.11
24.91
31.94
0.000
0.000
H
LINE :
28.169
30.611
28.835
23.729
27.392
27.836
27.725
35.384
27.725
34.052
27.503
27.947
29.612
30.167
35.384
32.831
31.332
22.397
32.831
22.952
29.945
29.834
13.850
44.930
SUMS
0.000
0.000
0.000
0.000
0.000
0.000
27.750
0.000
0.000
0.000
0.000
0.000
O.QOO
32.690
0.000
0.000
0.000
0.000
0.000
0.000
0.000
31.940
0.000
0.000
LINE
28.635
33.544
29.974
19.711
27.074
27.966
27.743
43.138
27.743
40.460
27.297
28.189
31.536
32.651
43.138
38.006
35.998
17.034
38.006
18.149
32.205
31.982
-0.146
62.325
ASHLEY CRESTED 8UTTE
**»*»»***R egress ion Output:
Constant
Std Err of Y Est
R Squared
Ho. of Observations
Degrees of Freedom
X CoefficientCs) 11.10
Std Err of Coef. 5.20
*****»"*ASHLEY CRESTED BUTTE
Regression Output:
Constant
Std Err of Y Est
R Squared
No. of Observations
Degrees of Freedom
X CoefficientCs) 22.311
Std Err of Coef. 0.341
DAILY
11.63
7.66
0.19
22.00
20.00
SUMS
•4.603
0.057
1.000
3.000
1.000
Data for Figure 2.
E - 8
-------
APPENDIX F
PROPORTIONALITY DATA AND ALL RAW RUN DATA
FOR EACH AK-18 TEST AT RESEARCH TRIANGLE PARK
JM138LLAPP
-------
TEST
SH-1
WM1381AAPP
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Tl
I
Crt
PC
I
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
177
177
237
297
357
417
477
537
553
SWEET HOME Units l=metric,
flK-18 2=English:
ES Y, DGM:
9-21-89 Pitot co:
SH-56-lfl Gas MW :
Pb (mm, in. Hg):
573.00 Stack area (m2,ft2):
Wood moist <.'/. uet):
39.00 Burn
vel dp
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
040
040
040
040
040
040
040
040
040
040
040
040
stack
temp
(C,F)
98
97
98
96
108
99
98
101
101
101
93
93
DGM
rdg
(m3,
41.
69.
95.
120.
120.
146.
173.
199.
225.
252.
278.
284.
ft3)
801
300
500
358
584
600
200
500
800
000
000
951
DGM
temp
(C,F)
81
103
109
111
100
99
100
100
99
97
97
97
Samp vol
2 (sm3,scf)
1.007 230.487
0.99
28.56 Flou rate
29.74 (dsm3m,dscfm)
0.1963 145.77
18.64
rate (dry kg/hr): 1.51
DGM dH
(mm H20)
(in.H20)
0.800
0.610
0.600
0.600
0.600
0.600
0.600
0.600
0.600
0.600
0.600
0.600
vel
(m/min)
(ft/min)
823.19
822.45
823. 19
821.71
830.53
823.93
823. 19
825.40
825.40
825.40
819.49
819.49
PR
(2)
111.3
102.1
100.4
ERR
101.1
104.2
103.5
103.2
103.0
101.1
102.1
dDGM
vol std
(m3,ft3)
26.917
24.631
23. 123
0.209
24.589
25. 186
24.857
24.857
24.807
24.706
6.605
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
823.61 98.58
-------
Method 5G Proportionality RatG, Flou Rate,
Burn Rate, and Sample Volume Calculations
I
co
PC
I
Stv manu:
Model no:
Lab name:
1st date:
Run
1st
no :
time
(min):
SWEET HOME
flK-18
ES
9-21-89
SH-5G-1B
573.00
Chrg ut
(Ib
uet):
run
time
(min)
0
60
120
177
177
237
297
357
417
477
537
553
39.00
vel dp
(mm H20)
(in.H20)
0.040
0.040
0.040
0.040
0.040
0.040
0.040
0.040
0.040
0.040
0.040
0.040
Units l=metric,
2=English:
Y, DGM:
Pitot co:
Gas
Pb (mm, in.
Stack area (m2,
Wood moist C
106.1
101.3
96.5
ERR
103.8
104.5
104.6
104.7
105.0
103.3
105.3
dDGM
vol std
(m3,ft3)
29.365
27.952
25.396
0.000
28.864
28.877
28.731
28.826
28.921
28.877
7.792
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C8F)
823.61 98.58
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED Q -Z/-
DATE RETRIEVED
- T.1 -
PROBE
LINE
CONDENSATE
1.0
TEST LOCATION.£5 Ll)S £AJ,
SAMPLER SN# "^ */ f $, *]
TEST TIME $"5~3
BL.AA) 7"''-i t 5" 73
FILTER?1 —
FILTERS
(MIN.)
35.
(HG BAROMETER UNCORRECTED)
PRETEST B.P"29,?2.(IN HG)
TANK 7 9. "7 5 (—IN HG) TEMP.
TORR ABSOLUTE
TOTAL (MG)
I/ (C)
+ o ,y
7.6
STOVE I
WOOD SPECIES
WOOD MOISTURE (% DRY) "2.1.9/
WOOD MOISTURE (Z WET) / g. <
POSTTEST B.P. 7.
TANK /<^ . 5"
(IN HG)
SAMPLE FLOW RATE PRETEST
RQT3METER <^ g^ = (ML MIN) 6 Q
(—IN HG) TEMP. 7.
(C)
POSTTEST
ROTAMETER^O =(ML MIN)
TORR ABSOLUTE 33/^2-
PRETEST LEAK CHECK
START <^.Q (IN HSO) FINAL $.*} (IN H20) LEAK RATE O - / (IN H20 MIN)
POSTTEST LEAK CHECK
START V, ? (IN H20) FINAL fr?/ (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS :
C02(%)
7o
02(%)
.' ^> 7
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
MIN.
MIN.
MIN.
DELTA
PROBE+FITTINB
SAMPLE LINE
CONNECTOR
3V.V /./„
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED 9 - "*• /~ # 9
DATE RETRIEVED °) - 2"Z-g9
TEST LOCATION ^5 bl $ 4 •
WEIGHT GAINS
PROBE
LINE
CONDENSATE
FILTER01
o.V
SAMPLER SN#
FILTER#2 —
TOTAL (MG)
(HG BAROMETER UNCORRECTED)
PRETEST Z.?29,92. (IN HG) ~
TANK 2. ?, g c (—IN HG) TEMP.2. / (C)
TORR ABSOLUTE 3 * #
POSTTEST B.P. "2 y,^/ (IN HG)
TANK /&>.~)C> (—IN HG) TEMP- ~i / (C)
TORR ABSOLUTE *%
TEST TIME 5" 53
fit.sj
STOVE
(MIN.)
WOOD SPECIES
.^r.^s
% DRY) "Z2..
WOOD MOISTURE (%
WOOD MOISTURE (% WET)
9/
WOOD CONSUMED (LB)39.0
SAMPLE FLOW RATE PRETEST
RO'faaETER (, %" =(ML MIN) <^Q
POSTTEST
ROTAMETER ^ / =(ML MIN) 5*5
(IN H20) LEAK RATE &•/ (IN H20 MIN)
PRETEST LEAK CHECK
START ^, 2- (IN H@0) FINAL_^_
POSTTEST LEAK CHECK
START <£. / (IN H20) FINAL 5-9 (IN H2) LEAK RATE & •> 1- (IN H20 MIN)
POSTTEST GAS ANALYSIS
co2(%)
RUN COMMENTS; $ ff #1 5
co(z)
02 (Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
^/ MIN. +>/oMIN. +>d/£7MIN.
DELTA
PROBE+FITTIMG
SAMPLE LINE 37.
37.
O.CJO
o.
CONNECTOR
F-SH-1-4
-------
Page.
CLIENT A
ES PROJECT /?P /2-3
PARTICULATE WEIGHTS SUMMARY
RUN No. a+.a/Ti
STOVE MODEL No. /)k~ / *£
POSTEST
.of.
ine_
\00
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
^-ZV
o ^y*-)
9 ---2-5
/o 7, ^
9 -2S
• I *?;&
*i-n
FRONT
KTF.TRR it
$4f-S
oizoy
e/101 <%„
^L.£f%
O/-LOD
' 1 2,6 &
0 /206
— £> ,&t>6&>
BACK
FTI.TRR U
5"^-^
* /2/y
• /^C9
«/?/5
* /z/-?
o/ZO^J
O-O6&Y
CALIBRATION WT.
WT AMOUNT =
PRE WT
«y99T
f .)oitfj
* 6~ao
POST WT.
» 5 (?&/
*y9i<]
* S?;
?.9-^
Initials
t
/*f
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY ' Page of
RUN No. gT//-///'/'V/7 Placed in Dessicator: Date/Time ? -2?-??
STOVE MODEL No. flK- / ¥
POSTEST
Acetone Lot it 9// ft,
Acetone Sample Volume.
ci
WT 1
NT 2
WT 3
WT 4 -
WT 5
FINAL WT
f
TARE WT
NET
DATE/TIME
<9-2 V
e>6 3o
f - T-5
' //?,<
9-/£
BEAKER it
A-5
(oc6, G>6%^
63,66 ^3
b^.tpC**^
&$. 0&I3
c> t oo7o
CALIBRATION WT
WT AMOUNT =
PRE WT
^&j OC6Ci
6~o > £*-*<>£•
^
POST WT
V9. 999
BAROMTRC
PRESSURE
T.^^<;
±^-c/S
Initials
fC^
S*c%
I
en
ffi
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED = .
0, oolo
TOTAL PARTICIPATE CATCH (A+Bn-C) -
0006?
-------
CLIENT .
ES PROJECT
O J~£
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No.U^V/'^/-//^ Placed in Dessicatoi-: Date/Time.
STOVE MODEL No.
POSTEST
WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE WT
NT GAINED
DATE /TIME
O 9V7
<* -Z5
9- "2-5
IS to
?-n
•
FRONT
RTLTRR It
SHt -7
• iz/y
./Z/3
-y?_/^
*/2/?
./2o*
^.^0^5
BACK
RTf.TRR if
&£**
o /~Lc~3>
.flo*)
•
9-/S
BRAKER It
/?-£'
&<&>5$o%
(,%,5S0<1
63 . 5 5o
POST WT
4^9795
^ , wn /
ROOM CONDITIONS
RELATIVE
HUMIDITY
6%. '
V6 ^& %
BAROMTRC
PRESSURE
•2L?.?6
•2^9^
Initials
/^/^
fa*f
I
to
ffi
I
t—'
I
CO
(BLANK CONC.) x
(ACETONE SAMPLE)
WT GAINED =
6. o & 3
a O
ms.
-------
CLIENT E Pfl
ES PROJECT /? O )
PARTICULATE WEIGHTS SUMMARY ' Page L of—/
RUN No. 6 VS
9-2-S
//Z*/Z
I
en
PC
I
O,0
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED =
f>.tnj/(f (C)
TOTAL PARTICULATE CATCH (A+B+C) =. ^7.3
rog.
-------
/ o£.Z
CLIENT
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page
RUN No.^fl^l/^L Placed in Dessicator: ftate /Time °? - "2-Z. - 3 «Ks//
STOVE MODEL No.
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
NT GAINED
DATE/TIME
Q,-7 V
6? o53o
q - "z 5'
lo^fj
9-r?
FRONT
PTr,TRR n
/?^-5
*7/o5
.7/^>^
-
.7/otf
*^7^9<^
i-9.$7^
Initials
t
strCj?
t*\
I
CO
rs
i
(A)
(B)
-------
CLIENT _£
ES PROJECT RP / 23 STOVE MODEL No.
POSTEST
PARTICIPATE WEIGHTS SUMMARY ' Page ( of
RUN No. ZA/'R- Jfi Placed in Dessicator: Date/Time ?"2f~89
Acetone Lot tt Iff O
Acetone Sample Volume.
WT 1
WT, 2 .
NT' 3
WT 4 -
WT 5
FINAL WT
j
TARE WT
NET
DATE/TIME
9-2Y
/? // V<
4-25
y/z<
•
^f- /^-g*1
BEAKER K
A-^
7^>,7o3^>
..7*/7oZ9
7 o . 7o Z ?
*70 ,7^/3
o , O J
SA.OOC.O
ROOM CONDITIONS
RELATIVE
HUMIDITY
5o@>& ^ .
yc®&~)
BAROMTRC
PRESSURE
29-?£
7'^.t/K
Initials
/)*£/?.
^c/$
•
I
CO
BC
I
(BLANK CONG. ) x
(ACETONE SAMPLE) - O -O
WT GAINED = ff y-r
6- 00 ft (C) /'/
TOTAL PARTICULATE CATCH (A+B-t-C) = V 3 . # me.
-------
CLIENT _£
ES PROJECT /? D
PARTICULATE WEIGHTS SUMMARY Page
RUN No. $//"£'<£ -/ Q Placed in Dess icator:
STOVE MODEL No.
POSTEST
/ of
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
9-ZV
o ^H^
q- zs
<7-/7-*l
•
FRONT
RTr.TRR U
K^~~J
» 1 / S °i
f, *~j / & <7"
/ / o O
. -7/sr
..5.7
£^ * o ^o /
BACK
FILTER It
A £-S
f (i>a (f i
O U) C* (ff O
.(MV
* 6> D 2, ~~t~
& i Q& r V
CALIBRATION WT.
WT AMOUNT =
PRE WT
a fTooi/
• w?
POST WT
* 797^
-v^y
ROOM CONDITIONS
RELATIVE
HUMIDITY
$o&tfi
V&&67
BAROMTRC
PRESSURE
7<7t
Initials
g
*cj
WC{(
•
ffi
I
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
- Run * '
ES Project i RQ /Z 3
"Wood Heater Model
Operators f/J
TEST RUN INFORMATION
Attempted Burn Rate (*g/fcp-)
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.
Actual Fuel.Charge Wt.
Pretest
7*5
0
O, 600
Post Test
TEST FUEL DATA
to
Coal Bed Range Wt.
Actual Coal Bed Wt.
Fuel H2OS Dry
Fuel : Dry Kg
to M
"7
Wet
LOADING/TEST START OPERATIONS
By-pass /Q^So-Cy Air Settings
V '/
Door cu^y^ 'I, Comments
Velocity Traverse
p Temp
A 1 6,635 ICO B
Ave. p
Pitot Leak Check
Static
F-SH-1-13
-------
Qmata
ENGINEERING-SCIENCE, INC.
CHunt
Date
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Run H
/-I -
Wood Heater Model
Test Fuel Charge
Coal Bed
Page 2- of
ES Projec^ f /?/? /T.3 Operators AJ |-j ("f
I
CO
33
I
Time
Sampl i ng/
Clock
/55V?
1JO_
18.10
Test
:uel
Wt.
(Ibs)
3O.
2=*3=
Flue
Draft
(in
H?0)
.0^/0
Comments
A 6'
22£
Catalyst Temp
Pre
6Z&
9/7
nternal
net*
158
968
Post
97
9-7
"522
V-V3
V76
Surface Temp.
Rear
3ZZ
3/3
30 S
799
2.9-7
22?
34V
Uottom
35 z-
•3*?
35/
3V?
•355
tight
^L
Vo?
Left
122,
:2Z3_
550
Stack
5^37
53^.
537-
W?
Oil.
Tun.
Tem
/GO
loom.
Temp.
a -?
57
87
^2.
_1Z
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client tL9f\-\lPT Run
Dat
ES.Projec, f fffl y7_3
Wood Heater Model
Operators
Test Fuel Charge "7./2,8 J3*S Page J__ of ^
Coal Bed 2. .1
i
to
PC
I
Time
Sampl i ng/
Clock
1(0
-?, 1
I 2. 3
1 2, 5
(3 f
I'b-f
Test
Fuel
Wt.
> f Ci
Flue
Draft
(1n
H?0)
6,0^2.
Comments
15. V /•?>.-*=.
idlckt-eY
Catalyst Temp
Pre [Internal! Post
1(67
9-33
IC./0
mn
I/ /a
fllO
(JW
76
5(2
$7?
•$76
5 c fe 7 &
Surface Temp.
Top) Rear| Bottom |Right| Left
277
353
^•70
3C2.
3V9
333
337
S3 &
J5W_
Stack
Temp.
V^
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater /MC-lft
Date
Samf
Samp
Run
; ^-"t-l — "^^
>ling Locat
>le Type
ion ^-f 4 T^_
tASfo—
T~l IT "™* T,'tBjrJ" V r~T~
Start Time 1 «^ -^
Stop Time
Probe Length and
Pi tot Tube Coeffi
A Assumed Moisture
Operator uiVU-V ' / \
Ambient Temperature
Barometric Prf
Static Pressur
Filter Numberi
Meter
;ssure
•e, (P.)
s)
(AO 1H
Type . /'? tf W^^
cient *.i°)
^/
Sample Box Number
Meter Box Number
fT-3 ^- -3,
Meter H
Pretest Leak Rate • o,O| "Z_ L
} ?& Z-1A
~3c> /"Z.1>3
V O ( 7^<-/ 3>
5-0 / -2X ~\
f*.0 t.C-1,
-70 l?> I^S
B^ 1^7^
fe>G "3 "/"*>
i/r> /•*>«=, 3
/T.O /^yo"^
/3° t<-J t ~~*~.
/^>0 /u -i, ~h
1 (oO [t-f£-f~\
I'JO ^<-f c^ ~\
~J-&£> n~) t5o o
-A^-fc \T? 9"2^o
/A7 rs~3o
— ^-fJ? : — ffif.C'
Gas Meter
Readi ng
(Vm) ft3
jytfti i
5|, (
5Zc"O
^,0L<,
d.^^
<^9f ."^
-73. £/
"71,7
_,^,5#
;7o,52y
/ E-Vi "7
; --2-2 C?
) _•> >j *:>
Velocity
Head
( Ps),1n.
OiCx^O
c>,,o HO
o^o ^o
G.^V^
o>,o<-/O
, OL/O
4> . '^ '-/if)
i o^/d
1O*-/O
-c^cyCi
. ,C*Cf o
\O^YO
.0^/0
tt> Vf ^
-t
. <3 V/^
,oVo
{£>"-/£>
^ cwo
^ <2>'-yo
_i^^ —
, <^^/0
Orifice F
Differe
( H), in
Desired
i^O
^
'ressure
jntial
H^O
Actual
•So
~ .-70
ifi>O
/*7 ^
,G6-
f/r/
• ^ 7
^~" Q^i
•^£>
I'Sft
( [ ^ L'
V ( O C J
060
* 6>o
r £)
i &±O
\ fer>
. /"/^o
.. Sa O
TEMPERATURES
TJMvT0"
Meter
In
^/
Meter
Out
g 1
<§c/
AT
9^
/&3
/<>3
/n <>
/D'T
y6©
/OP
fc> iT
'^t
///
^?-
(( |^
/oO
^
1 — 4*9 J
Filter
c>/\
/j C_x
Impinger
^>2_ (i? "^>
£3 p (p /
^2. 6^
$2- £o
A/ /
§2^ 6 c-/
r8? "^ (/o'S
G,"^
^"^
f r
^^ 6"!b
t5'!S /^Z>
S^
57
<*=? 7» 5<^
J?4^ -'"'"*'
^x — ^?—
Pump
Vacuum
1n. Hg
'2_*^
"Z—Q
%"^\ cD
*^s ^
"S^
-*•>,&
"^-<9
3.6
•^,a
3>C>
"b>O
3.o
3-O
O>.e>
"3x(3
13,0
•Z-.5
"2< *>'
z<^
^jg:
Flue^Bfaft
a-ru H9o
-. •
[
S^z g"?S 1 g--r=S 1 C
-------
ENGINEERING-SCIENCE, INC.
Client.
Date
-&]
WOOD HEATEIl CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Page > of
ES Projecv | R£) /Z3
Wood Heater Model
Operators
PG
I
Time
jampl i ng/
;iock
X L/o
2 rt
7000
(3 •Co
-/00
'LI 1 O
~7J
Test
Fuel
wt. .,
(Ibs),1
Q.cs
o.o
Flue
Draft
(In
H?0)
0.65
6056
Comments
\,Z
Catalyst Temp
Pre
m
7*5
nternal
//OS
/Z70
me,
Post
/o?
/^8
(60Q
03 /
Top
111
Surface Temp.
Rear
5/S
•3YS
3/3
Uottoiu
35C
35-9
33-7
Ri ght
Left
Stack
Temp .
632.
£03
5V ^
on.
Tun.
Temp .
99
/do
la/
/(TO
^oom.
Tem.
SC4T
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
'Date
Ak-
Sampling Location
Sample Type
Run Number_
Operator u.
°l-1.{ - Ps9
tTT
(4- - f? fi- - f A.
Cl
Sampli ng
time, min
ock Time
24-hr
lock)
Gas Mater
Reading
(v) ft3
Velocity
Head
UPS) in
H?0
0,0 HO
Orifice Pressure
Di fferential
(AH).-in. H20
Desi red
Actual
n
TEMPERATURES
Dilution
Tunnel
Meter
In/
Meter
Out
Filter]Impinger
Pump
Vacuum
in. Hg
Flue Draft
n. H?0
/.
"2
7
-4-
('DO
/PO
101
-7
l"l i
tol
-3
V
6p
X^L.
EC
I
I
CO
0,
/GO
-2-
SI
VC?D
I ft O
D
fern
£-0
7
160
90
7
n^o
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
Date
•A
Sampling Location
Sample Type
Run Number
Operator
t^T"
^\ Clock Time
SamplingX(24-hr
time, min\£lock)
" ' — • — — — — —
Q^n 7£rtso
^/^-? -2.0(0
<-( "1 7 • ~?£> 7,0
u a~7 2.0 -3,0
t-f0?1] 9j=>VD
507' Zo^o
15 f -7 -2-/00
T2T7 -7.MO
5 "5 *7 • "2,1 2,.o«-t?(i>
G^O^O
OcO""^
o.DVO
O.of^
^<°5fc>
OiOCrO
diO$»
A^aVo
o^OYo
-£>• O^p
Orifice P
Different
(AH), -in.
Desired
\(f&
,6o
cC*0
GO
VC,C)
' , Co
e£O
,^<9
i<:.0
tCa.O
ressure
ial
H20
Actual
1 (oft
• foO
^6>O
i r"oO
sC^n
vC?o
, ^o
i6
^^0
L(JLD
-^0^
TEMPERATURES
Dilution
Tunnel
s^~~
1
J-
V
x q^.^
Meter
In. *
/
o /
^Q
'T
7f
7^
Impinge'r
3^
<5ft
^A
^fi
5"A
^•-7
^^
^-*^ Q5
5 O
•5 A
5-f
-
Pump
Vacuum
in. Hg
•7, CN
2,-o
2-o
Z-o
z, d
2,0
Z^o
2^o
^^o
^ n
Flue Dra^t
in.^H^D
s*
•n
I
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING OATA
Sampling Location
Sample Type
Run Number_
Operator
Start Time
Stop T1me_~
•a (A -
Ambient Temperature ~
Barometric Pressure
Static Pressure, (Pq)
Filter Number(s)
Meter V— UO2>-/
Probe Length and Type_
Pi tot Tube Coefficient_
Assumed Moisture
Sample Box Number
Meter Box Number
Meter H
Pretest Leak Rate a.oo-^
Post Test Leak Rate 0,00 £,
Gg;
Read and Record All Data Every lO Minutes
Clock Time
Sampling (24-hr
time,min Clock)
Velocity
Head
( PS),in-
H20
Gas Meter
Reading
ft3
Orifice Pressure
Differential
( H). in
r\~. ~J~.~ . ' I
Desired | Actual
TEMPERMURES
fe)
^
Tinffel
Met
Meter
Out
Filter|Impinger
Pump
Vacuum
in. Hg
/o
9o
"3^0
vo
/ 2-^3
o.
-3,0
•3.0
393.
-70
T..O
LuS.
/OO
-90
Htfi,b
0.0^0
. o
20
• fo
85
-so
/ZZ.
pit)
•3-6
no
a
"1
<*•=*
O
,9-7
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
Date
Sampling Location
Sample Type |
Run Number
Operator
Crr
5 H -
^\^ Clock Time
Sampling\(24-hr
time, min\£lock)
Gas Mater
Reading
(Vm) ft3
Velocity
Head
UPS) in.
H?0
Orifice Pressure
Differential
(AH).-in. H?0
Desired Actual
TEMPERATURES
Dilution
Metei
Meter
Out
Filter)Impinger
Pump
Vacuum
in. Hg
Flue Dpaft
1>^»20
~L1T\.
(O
9
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater /t(/_ ^ te
Date
<^?— '"2-C -^(Jf50^
Sampling Location 1^>T & ~2__
Sample Type
tA^Cr-
&<* 3/3
Run Number 'T) V-} - ^ 6~ ^- 1 ^ J
Operator / ^ vV ^V
•
•n
i
CO
1
*— •
1
NJ
K >
\. Clock Time
Sampling\(24-hr
time, mi n ^vClock)
~~ " ' — — — — — .
^^7 ^50
VS "7 ~2js> &o
Y^7 ^°
H~17 701^
c/^7 2o3c9
•^97 ?ot-/c>
^So 7 2,c\ S rt
^ i"~) "LLCrO
5 2 -7 "2-1 I o
G"? "7 2-/ 2.0
5 Y7 "2-' ^^^
£^ i-» ~~t, «*7 1 ""5 /**
— •* • -^i * * S/^
*-/
^"7, ^o<-/c>
dtC/T'O
<^>LaVc)
^cOt-/e)
O^'tf (^
Q^O1-^ O
O-O^V O
^5 ctixy^)
c> , o y o
Ori f ice Pressure
Di fferential
(AH), -in. H20
Desi red
,"75
.9S"
rdy^'
^S
,95
.1S
, ^S"
> ?5
v^ -5
v^^>
i ? 5
Actual
L ^5
9<^
i ?S
tl "S
^ *r <^
•9s
. *V "S
i ? ^
i ?"!>
j 9^5
i ? 5
TEMPERATURES
Di lut ip-n
Tunne^T
/
Meter
In/
-
Meter
Out
/6 'S
/6"5"
/oc;
/•o "S
I At-l
/&<-1
/fl'y
l&t—i
(OH
u-j w
Filter
r9 ^/
c?y
ftif
£)<-/
fit/
(,>
Sr>^~?
&> 7
<£ A
6 "*»
6 •?
"^ *^
3ump
Vacuum
in. Hg
^c^
^_ o
3,0
~b-
3.0
3"-°
"3..£>
-7.0
"3, a
-7.0
O^O
Flue Draft
in. Hg0
/
-------
FUEL MEASUREMENTS
Date _ ^--"Z-^ —B 7 Wood Heater Manufacturer
_
Project No. _ Woocf Heater Model A l£ -/
Run No. ^ U_ I _ __ _^
Circle One: C^retest Fjjgl / / Test Fuel
Fuel Type and Amount 2x3 ^-"^ 4x4 _ 1x4
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length . -7 _ . _
Moisture Meter Calibration 121 _ t2,*.q 22S -2_.2-<
°p -7 • :
Moisture Content- (Meter - Dry Basis)- ConvecTtd.
Piece No. Readings Average
2
3
4
S
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Overall Fuel Moisture Average
F-SH-1-23
-------
FUEL MEASUREMENTS
-2T
*3
Date 1-
Project No._
Run No. s
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
Fuel Piece Length f "7 *-f
Wood Heater Manufacturer SiVJsT~t—.
Woocf Heater Model
4x4
Tefwef
"*— 1x4
.Actual Load Weight
Moisture Meter Calibration 12%
"
22J
Piece No.
1
2
TIT
11
12
13
1*4
15
16
17
18
19
20
Moisture Content- (Meter - Dry Basis)-C°'v'*:'7°t
-------
TEST
SH-2
WS\RD12340
RJM1381AAPP
-------
Method 56 Proportionality Rate, Flow Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: SWEET HOME
Model no: flK-18
Lab name: ES
1st date: 9-28-89
Run no : SH-5G-2R
1st time
(min): 615.00
Chrg wt
(Ib uet): 20.50
run
time
(aim)
0
60
120
180
240
300
360
420
480
540
600
615
vel dp
(mm H20)
(in.H20)
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
Units ^metric,
2-English:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.7. uet):
Burn
stack
temp
(C,F)
81
81
83
85
86
89
86
86
88
82
80
79
DGM
rdg
Cm3,ft3)
290.402
320.300
350.300
379.900
409.800
440.000
470. 100
500.400
530.800
561.600
591.100
599.547
DGM
temp
(C,F)
68
86
90
90
91
92
91
90
96
90
84
81
Samp vol
2 (sm3,scf)
1.007 302.303
0.99
28.56 Flou rate
30.12 (dsmSm.dscfm)
0.1963 150.52
18.33
rate (dry kg/hr): 0.74
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
H20)
H20)
800
800
800
800
800
800
0.800
0.
0.
0.
0.
0.
800
800
800
800
800
vel
(m/nin)
(ft/min)
815.43
815.43
816.93
818.44
819.19
821.44
819.19
819.19
820.69
816.18
814.67
813.92
PR
(*)
102.7
100.0
98.1
99.1
100.4
99.0
100.2
101.0
100.0
97.0
112.3
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
30.
29.
28.
29.
29.
29.
29.
29.
29.
28.
8.
std
ft3)
356
455
851
143
382
232
480
631
697
753
324
vs/VmTs
.00
vs ave stack
ave temp
(C,F)
817,56 83.83
I
CO
PS
I
NJ
I
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
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
615
SHEET HOME Units l=metric,
flK-18 2=English:
ES Y, DGM:
9-28-89 Pi tot co:
SH-56-2B Gas MM :
Pb (mm, in. Hg):
615.00 Stack area (m2,ft2):
Wood moist C
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
'?
• S
WEIGHT GAINS
DATE DEPLOYED 9 -
DATE RETRIEVED
TEST LOCATION (~ S~
SAMPLER SN* ^ V/ 6 "7
(HG BAROMETER UNCORRECTED)
PRETEST B.PgO. "2.5 (IN HG)
TANK 3 O • / 5
PROBE
LINE
CONDENSATE_
FILTER*1
FILTER*2
TOTAL (MG)
^.^
RUN*
0.0
TEST TIME 6l S (MIN.)
STOVE ID /) /< - X V
WOOD SPECIES Do {_£
("IN HG) TEMP.JV_(C)
TORR ABSOLUTE J2. .
POSTTEST B.P- 3o.
TANK /3 ,
(IN HG)
WOOD MOISTURE (% DRY)
WOOD MOISTURE (% WET) '8>'5'3>
WOOD CONSUMED (LB) IQ^ (KG) '"f.
SAMPLE FLOW RATE PRETEST
ROTflgETER (f *& =(ML MIN)
(—IN HG) TEMP.Z-/ (C)
TORR ABSOLUTE
POSTTEST
ROTAMETER_£_£_=(ML MIN) S 3^
PRETEST LEAK CHECK
START
(IN H20) FINAL3- *T (IN H20) LEAK RATE O ,\_ (IN H20 MIN)
POSTTEST LEAK CHECK
START 5. E) (IN H20) FINAL^^ (IN H2) LEAK RATE Q ,
1_ (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
C02(%).
C0(2)_
02(%)
b
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE+FITTING
SAMPLE LINE
CONNECTOR
+37 MIN.
+£
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED
- 89
DATE RETRIEVED
TEST LOCATION £<,' £J S - L/)
SAMPLER SN# 9 *5 3 . S
WOOD MOISTURE (Z DRY)
WOOD MOISTURE (% WET) i g1, '?>
WOOD CONSUMED (LB) c^-S
SAMPLE FLOW RATE PRETEST
ROTQaETER & % =(ML MIN)_
POSTTEST
ROTAMETER $£> =(ML MIN)
PRETEST LEAK CHECK
START
(IN HSO) FINAL?.*? (IN H20) LEAK RATE C . *? (IN H20 MIN)
POSTTEST LEAK CHECK
START V. $ (IN H20) FINAL<-W (IN H2) LEAK RATE Q ,, / (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
co2(%)
com
02(Z)
PRETEST
SAMPLE LINE
CONNECTOR
- MIN.
MIN.,
37,/V.
DELTA
000
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
F-SH-2-4
-------
CLIENT L r _ _
ES PROJECT flD
PARTICIPATE WEIGHTS SUMMARY Page of
•
RUN Ho. <5M-(JPT~~LAPlaced in Dessicator: Date/Time 9-3*9
STOVE MODEL N
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
q-~*>e
H* /t>
lo - z.
li> i s
5
0 t~Lt(e
d.oe/q
BACK
Fir.TER If
S*£--i*
./•Zo?
. /^^c
.not,
•/Zo^
~ OiOOtt-
CALIBRATION WT.
WT AMOUNT =
PRE WT
• y^*?
, <5eoo
POST WT
. 5"otf 7_
. V9<7?
ROOM CONDITIONS
RELATIVE
HUMIDITY
Vz(^?7£>
C^^76
BAROMTRC
PRESSURE
29-9V
79- ^
Initials
l
/M
I
(A)
(B)
-------
CLIENT ^
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. ^/^~/)PT- 2/ff- Placed in Dessicator: Date/Time.
STOVE MODEL Nc
POSTEST
Acetone Lot it
/
//
.
Acetone Sample Volume 5 C?
WT 1
WT 2
WT 3
WT 4 '
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
/>/ <(
•
1-/1-91
BEAKER II
/9 - Z7
CK.aC,-)-*,
££.^77
6>t.n67~J
™'°"*
O.OOK/
CALIBRATION WT
WT AMOUNT -
PRE WT
y9 ^9
60 666 /
POST WT
^ '9, 9979
^ 9
-------
CLIENT
ES PROJECT A0 /Z>
PARTICIPATE WEIGHTS SUMMARY Page of.
*
RUN No J?/'-^-^ "?/*? Placed in Dessicator: Date/Time.
STOVE MODEL Nc
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
9-3°
fl*)a
)t>- Z_
fa > ^
9-77^
FRONT
FTF.TRR It
Sy&f-Z^
.llo<&
.11^*1
• I'Loq
*/Z./o
"O.oool
BACK
FTf.TER It
5^-*o
«//^6
. 1177
, ffoc&
POST WT
• *>f>a 1—
,£/Wi
ROOM CONDITIONS
RELATIVE '
HUMIDITY
V«B4j
BAROMTRC
PRESSURE
Z9-9V
Z9. ^8
Initials
i
We /?
sx.cs
\
I
Cfl
re
i
NJ
I
(A)
(B)
-------
CLIENT
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page of.
RUN ^G.^fl-OPT-T-P) Placed in Dessicator: Date/Time.
O
<»
STOVE MODEL Nc
POSTEST
Acetone Lot it.
Acetone Sample Volume
,*,, 9-??
56
WT 1
WT 2
WT 3
WT 4 '
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
q - 30
l@ — "Z.
'
TOTAL PARTICULATE CATCH (A+B+C) =.
_mg.
-------
, CLIENT
PARTICIPATE WEIGHTS SUMMARY ' Page of.
RUN Nn.*^- -^
lt>. S6*/*;
~)o . $6H~7
"?<>. 56V7
~?o .s^^o
0,fl<\ $7
CALIBRATION WT
WT AMOUNT -
PRE WT
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT
ES PROJECT ftO /23
RUN NQ.QV- -?l Placed in Dessicator: Date/Time 9-2^
o*-* •
STOVE MODEL No. /)M - t ^
POSTEST
WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
Q - 2>c-
V, z,^
lo - 1_
/e> -2*5
4 7-/7- ^
FRONT
FTF.TRR It
^2.7
• CQ&T-
. f^ty
.<^Y
-^8^3
0.6/V/
BACK
FTLTRR 11
4^-2sr
.6^o^>
,67^5
#^795
' (^71/<;
""^3,
BAROMTRC
PRESSURE
Z9-97
29- ^S
Initials
,
/*)<•*
s^p.#
\
I
CO
(A)
(B)
I
I—'
o
-------
of.
,CLIENT ^
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page
RUN Ho. C^-^X?-?^ Placed in Dessicator: Date/Time
STOVE MODEL N
POSTEST
Acetone Lot 0 ?// &
Acetone Sample Volume___£S
/v
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
1
TARE WT
NET
DATE /TIME
q- -to
h/s>
10 - Z
al ^6
()*/$- W
BEAKER it
/4^v
^^.^7o/
6 8 . t, 7o i.
fa^.&Jal-
(tK.b&S'Z
K.OoW
CALIBRATION WT
WT AMOUNT =
PRE WT
¥9- 977 , £>6C /
POST WT
^ <$, wf
v^.w^
ROOM CONDITIONS
RELATIVE
HUMIDITY
V*&?4 '
£>-2©&>~l
BAROMTRC
PRESSURE
•z 9-3 <7
'il.S'fi
Initials
SKC^
SkC4>
I
CO
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A+B-i-C') -
(C)
~LO.O
mg.
-------
CLIENT I
ES PROJECT /?/? /Z 1
PARTICIPATE WEIGHTS SUMMARY Page, of.
»
RUN No. SA^SSrlLZL 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
9 -3^
/C^<;
/o- -L
lo -*>o
9-/7- «?
FRONT
PTf.TRR If
/^-Z*)
.^,^56
^957
, ^^57
• £££/
0>£>l5(f>
BACK
KTf.TER It
/kf-3o
. (y^OO
.^8oZ
* 6 Stf 7^
-6 £o~£-
0. 600b
CALIBRATION WT.
WT AMOUNT =
PRE WT
. $00 /
. £<7 OO
POST WT
. V9^9
. V9^9
ROOM CONDITIONS
RELATIVE
HUMIDITY
ys@7^
SZ^.')
BAROMTRC
PRESSURE
29-97
29,5" ir
Initials
a
/n^
fljt#
I
CO
(A)
(B)
-------
client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
- Run i
ES Project I K-U 12-^
Wood Heater Model
Operators L.O ("T U-
TEST RUN INFORMATION
Attempted Burn Rate. (Jrf/hr) (p Secondary Air Setting
Achieved Burn Rate (Kg/hr) '.IK j Thermostat Setting
Primary Air Setting
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (J)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
Id
16,0
Post Test
- C1
1 c .0 -- /a .
TEST FUEL DATA
Firebox Volume (ft-)
Fuel Charge Range Wt, /Z,6 to 15.
Actual Fuel Charge ut />+ic*n t.
Coal Bed Range Wt.
Actual Coal Bed Wt.
to 3-
"3 > /
5 Fuel H20% Dry Z2.V5 Wet (
Fuel: Dry Kg I.S'lH
LOADING/TEST START OPERATIONS
By-pass ^V&yaJc' Air Settings
Door Q; [c
-------
ENGINEERINp-SCIENCE, INC.
Client
Date
UOOD HEATEIl CEKTIFICAT10N TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Page
Wood Heater Model /Mt'C& Coal Bed
ES Project | P^ | 2-3 Operators / p. f-|-l4
Time
Sampl \ ng/
Clock
69 So
lc
li 10
IUQ
^5_
Test
Fuel
Wt.
(Ibs)
;/,
il0-
i ra
l^
Flue
Draft
(in
H?0)
C.Q5C
6.620
Comments
-J
—•*-»> A
Catalyst Temp
Pre nLernal Post
v?
87 7
777
<^>1
/ZSV
(131
8 "72
71?1-/
/D3
W
/I/1-/
fa/")
^53
7/8
67;
767
lop Hear Bottom Right Left
Vv/
Vz?
Surface Temp.
27V
^97
•2,93
&3_
3t, 7
W.9
3/7'
27
z./ s-
2,7,?.
179
zas
sy
25L2
Stack
Temp.
57 y
rx32_
2^75
Oil .
Tun.
Temp .
_£/
Room.
Temp.
7V
7V
iiL
7.3
7Z.
72.
2Z
2i.
71
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
'ENGINEERING-SCIENCE, INC.
Client Pft Run
Date
5/V "
_ 9 - 2 # - *£ *7 ' Wood Heater Model /IK-J
ES Projec. f /?/? /&3 Operators /?// A^.
Test Fuel Charge
Coal Bed
Page
of
ta
i
N3
I
Time
Sampling/
Clock
Test
Fuel
Wt.
(Ibs)
7/6
O ,
7W
z,-/
Flue
Draft
(In
H?0)
O.C7X;
A 07,0
00 CO
6.^0
Comments
Catalyst Temp
Pre (internal
7o7
72.5
8*5 (p
/ri 7
/£><&!
99/
//
(7.C.Z.
ay;
Post
9/3
97?
S/o
•V/o
tm.
Tl/
Top
3/y
377
583?
Surface Temp.
Rear
/77
/5V
/Oo
70 /
20.^
Uottom
2 60
Z.7-/
2.7V
Right
'Z3o
Z'/O
z-yf
295?
3/V
Left
330
336
22.
ii
.'iic?
Yr?
Stack
Temp .
3d/
33 '
35A
**
'>>:>
'^22.
on.
Tun.
Temp .
Ss-
So
Room.
Temp.
7V
75"
7-?
76
-ZZ
77
77
77
77
77
^2L
-------
UOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £Run H
Date
ES Projec.
SU -1-
Test Fuel Charge
Page
of
Uood Heater Model /?/<-/& Coal Bed
Operators
Time
Sampl i ng/
Clock
nz^
1
/ft 2.5
*r
5"
lOfi?
_2^L
7,0 '
Test
Fuel
Wt.
(Ibs)
A.?
7,7
7,3
, <;
Flue
Draft
(In
H?0)
0.070
O.rl.
Comments
O
7. 'ft/
Catalyst Temp
llnternal
m
22Z,
•<
« V;
TiS
797
/£*> /
57
///I
Post
7/y
;/y
5 7?
S'So
$"7?
ffitfi
Top
370
39V
V/o
%
Rear
Surface Temp
'27V
7/9
Z/7
7/6
zz/
225
?- ,1
Uottom
7fr 3
•7.9
'*-*!>£/
High I
7V
3/.1-
'3/7
Left
-3/7
"36 ?_
332
35?
39 '1
Stack
Temp „
^
25-
3/7
320
3/
3/9
Oil .
Tun .
Temp.
OS-
'S -S
S gr
s?
37
JLL
Room.
Temp .
3-1.
I-?
££_
79
22-
79
7V
7-3
7'?
7Z-
72.
-------
ENGINEERING-SCIENCE, INC.
Client £ p/}Run
Date <=l~7-'d-fi'J ' Wood Heater Model /9J<~^^^
ES Projec. f
i
CO
1
ro
I
i — *
-j
Time
Sampling/
Clock
<2,/35"
"2 ! yS
~2J 5 K>
i
Test
Fuel
Wt.
(Ibs)
c ts
0' /
c.o
Flue
Draft
(In
H?0)
• 67.0
tCTi-6
»tfZG
XP/^3 Operators ^' ci/f
Comments
• ^2-.p,,o
Catal
Pre
K^
^T9
79^
n
/
/
A
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Page V of ^_
Catalyst Temp
Pre
K^-?s
^T9
-?9f-
nternal
If* /
I/C-T-
(a t S
Post
9^
9%<3
%J?',
Surface Temp.
Top
VY
V^
,~J>
Stack
Temp .
'53 y
"39/
V?
on.
Tun.
Temp .
5'o •
*c?
79 •
I
A
w.s
Room.
Temp.
';/
>/
v/
*
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampllng Location
Sample Type
Run Number
Operator
Start Time
Stop Time
Trr-o-
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
Meter Box Number
Meter H
Pretest Leak Rate 0.00£,
Post Test Leak Ratec,0lo (3?
Read and Record All Data Every Id Minutes
Clock Time
(24-hr
Clock)
Velocity
Head
( PS),in.
H20
Sampling
time.min
Gas Meter
Readi ng
Ori fice Pressure
Di f ferential
( H). in. H?Q
Desi red
Actual
TEMPERATURES
Dilution
Tunnl
Meter
Meter
Out
Filter Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H90
—t.
/<:>
M H"?
0
IT-
-12-
.Ao
76
_sj^.
5
S
•2-
SO
/2-2
?o
5y
_2_
!?, 0
6 5
So
3
SO
,80.
• SO
3
,80
fSo
"So
7
77-
£-
72,
So
/o
-------
SAMPLING DATA (cont.)
4
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date
Me-18
Sampling Location_
Sample Type
Run Number ^
Operator
^ Clock Time
Sampling"\(24-hr
time, min\£lock)
Gas Meter
Reading
(V.) ft3
Velocity
Head
UPS) in,
-M
Orifice Pressure
Differential
(AH).-in. HpO
Desired Actual
TEMPERATURES
Dilution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H?0
/
180
So
O.oW 1
.BeJ
S'o
6JJL
. o
75
80
7-5
5o
7s
75
5"5",
7
^L
-t
3(10
,73s
x/76./
i_2_
4-
o.o-//
_7JL
7S
2>3O
, '2-
So
9o
^L
/ft/5
n ,<:><-//
*%&
/ ^ -2
7¥
2^L
2_
So
VI
5"
3r
77
77
-------
BpsngEssa
Kbaa tisss;
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ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater
Date
- 7-
Sampling Location_
Sample Type -7 %•/
Number y// - <
Run
Operator
<-'/?
Sampli
time,
ock Time
24-hr
lock)
Gas Meter
Reading
(vm) ft3
Veloci ty
Head
(&PS) in,
H?0
Ori fice Pressure
Di fferential
(AH), -in. H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
90 '
Filter
7?
Impinger
5" -3
ump
Vacuum
in. Hg
'Z-
Flue Draft
in. H?0
97
79
/
7"*
90 -
-7
9
7/
o
* 0
7o
// 5"
-X
So
-2/25"
55LL
t±
r 8-0
,-30
5V
S
5/
7
c*//
I
10
I
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-------
ENGINEERING-SCIENCE, INC.
SAMPLING OATA
Wood Heater /VK-/O
Date 9 - -2.
Pi tot Tube Coefficient ,9_ej-
,TS
Operator l^v-\vt-
Ambient temperature
Barometric Pn
Static Pressur
Filter Number
Meter Y~
jssure
•e, (P.)
s)
- /, O '2-c7'
Assumed Moisture
Sample Box Number
Meter Box Number
H
* / i *?_ c "A ^ v A I
-<*J _> k^ — /NJOl^TC: ^\^
OS'N- /
Meter H
Pretest Leak Rate <5,c6(^ /> // "
Post Test Leak Rate e>cv? (^>// "
Read and Record All Data Every /o Minutes
i
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EC
1
1
NJ
1 — '
Clock Time
Sampling (24-hr
time.min Clock)
6 U-i-i
2 e) J / .S" S
3o I zoc;
V ^' / 1 / £>
^0 SZ.75
~?o /z '/^
^(j / -2 tt
q (i /~*)£> ^
/(X-, / 3 / 5"
uo /-*>7<;
/2.0 /? •* 5*
73/7 /iy *>
I^G /3 / Vn 4"
//^>r/ /V/<"
/7^5 /f/ 2'^
/5?o /V? /VV9
^rn? / V S"*?
^/r> f^-o^
"^2<9 yC/C
.? 7o y 5"2"'C
^-* ,£. . ,.f . _^3
Gas Meter
Readl ng_
(vm) ft3
(r-V^-O
kS I.4-/
6 56 1 °>
6>G> /f 1
6>&6>t O
6>~?o» Q
£ -?. /• ST"
6 %$ e 7
.£>C)0- (j?
/ <7 c, . c;
7^O, *y
76 5 i <-/
I/O . Y
"))<^f "2_
72.O<-i/
Q, <^<-r (
<^,,o'-(l
n i *"-//
& ,.^((
O (-*-/(
d-ci'-i (
C-Ov /
_/T«ioY/
0.0^/f
Orifice F
Djffert
( H), in
Desired
.90
• So
i?0
;C( O
o'yO
« 9r>
» 9
* ?o
. VO
tCfO
• Iti
t 90
,9o
* 0 o
, ^7^
., 9 o
i^O
t9c?
/ 9c>
, 70
< <7^
.^o
'ressure
>ntial
H20
Actual
4 ^O
'^O
vC7 O
• *?£'
O ^
•^ ^? t"7
. O xi
>9o
<" 9<^>
« 9o
( *>&
• 9o
«*79*o
.9^
, Cl (^)
c ?O
,90
•»9o
.'icJ
TEMPERATURES
Di lutiprn
Tunnel
/
Meter
•/
'
Meter
Out
(o $j -
*7O
7S
7*7
S
O
9l->
9"^
f)y
9v -^
Filter
<^c "9
A^ *7 € /^3
•
Impinger
^ ^ •
7 "V> ^ "S
*7i_ ff"J
7z -ro>
?z ^^r
77.
7 •?
5".
7V
si
7 V 5"Pi
7'V 5' '>
7V
7V So/
7V ^T
7fS <^" V
•"7^ Ci <^
7<<)
"3S
j^
•p
•7
jj
3
3
•-^
^
"^
"\
~s
1
^
•5
v.?
•~-j
"J^
"^
"7^
~z
'^
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
V/ood lleater_
Date
Ak-ie
Sampling Location
Sample Type
Run Number
Operator
SH -
Gas Mater
Reading
(vm) ft3
n
-------
E^§
D/\
ENGINEERING-SCIENCE, INC.
nruiitu ut\u\ ^UUIIL.;
Wood Heater /9 /< - / ft
Date
<=f - 2 gr - 3-9
Sampling Location £~5 - ^JS^ ^s^?^
Sample Type "?
-K/ /9$~/5"
5"3O ^^2^
$"^/o 3c-^<3 "Zo/^
S6> O '2.£ft2>
^7(2 ~i-/05
5*V9 *2//<
£'£0 Z/zY/
* &<-//
e o'-/f
<9 ° V/
o
« 7c
' « 9o
« "v* c?
° ?o
* 7c*
' ^^
e 9r>
^ •?<:>
* 1(~
c> *.
O ,^
ressure
.ial
H20
Actual
, <7^
' 9 c>
V ^ O
, q C>
' *? £
> C/O
t'? O
>?0
* 9 o
'*? O
• 7&
c,9 o
• 1 (^
1 7 o-
f c/£>
• 9o
/^?' '^
TEMPERATURES
Dilution
Tunnel
Meter
In
-
Meter
Out
99 -
9 •?
99
A-p
9 *7
9 ^
97 -
9 6
o 5
^(/
93
9>7_
9z_ ~
9/
^^ -
.
^7^*3
Filter
7 9
"79
7 ?
7 ?
7c/
/J
7 6>
•73
73
7 "2-
*7T_
7/
7/
7/
?<3
Impinger
^--»,
5"4/
5-^
"5" "^,
S (^,
5-y
fT^S"
^.S~
5"c^
95-
5V
5"^
$"5"
5" <
•
'3
Pump
Vacuum
in. Hg
^J>
•^
•^
73
3
^
^i
J3
-^
^3
.3
-3
•^
^
Flue Draft
in. H20
I
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-------
FUEL MEASUREMENTS
Date -~2£*> -Q Wood Heater Manufacturer
Project No. <£ 72-"^, Woocf Heater Model
Run No,
Circle One: rPretestfuef ^ Test Fuel
Fuel Type and Amount -- 2x4 \y 4x4 1x4
Ideal Load Weight _ ; _ Actual Load Weight
Fuel Piece Length
_
Moisture Meter Calibration 12% / 1 _ _ 22%
°F £~ to
9
10
11
12
13
1*4
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Piece No. Readings Average
l ^ f if,i/ Z7.-2, ^^.y
2
3
4
5 __
5
7
Overall Fuel Moisture Average
F-SH-2-24
-------
FUEL MEASUREMENTS
Date I
Project No.
Run No.
Mood Heater Manufacturer
Wood" Heater Model
&
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight '_
Fuel Piece Length tl
4x4 > Ix4_
.Actual Load Weight"
Moisture Meter Calibration 12%_
1 /»Tp. -r d f-^
/ -7
22*
Piece No.
5 ?£
8
9
10
11
12
13
1*4
15
15
17
18
19
20
Moisture Content- (Meter - Dry Basis)-Co'v'*c7"t
F-SH-2 -25
-------
TEST
SH-3
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: SWEET HOME
Model no: flK-18
Lab name: ES
1st date: 10-2-89
Run no : SH-5G-3H
1st time
(min): 605.00
Chrg ut
(Ib uet): 16.70
run
time
(min)
0
60
120
180
240
300
360
420
480
540
600
605
Units l=metric,
2-English:
Y, DGM:
Pitot co:
Gas HW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Mood moist (.?. uet):
Burn
vel dp stack
(mm H20) temp
(in.H20) (C.F)
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
93
83
83
83
84
83
83
81
79
80
90
99
DGM
rdg
(m3,ft3)
603.308
633.500
664.400
695.500
725.800
757.000
787.000
817.400
847.500
877.300
907.500
910.045
DGM
temp
(C,F)
74
89
94
95
94
93
91
92
91
91
91
91
Samp vol
2 (sm3,scf)
1.007 293.332
0.99
28.56 Flou rate
29.57 (dsm3m,dscfm)
0.1963 150.77
18.48
rate (dry kg/hr): 0.61
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
vel
(m/min)
(ft/min)
842. 14
834.49
834.49
834.49
835.26
834.49
834.49
832.95
831.41
832. 18
839.85
846.70
PR
101.2
101.6
101.4
98.8
101.6
98.0
99.3
97.9
97.5
100.5
102.4
85.49
17.640
460.00
1850.00
dDGM
vol std vs/VmTs
(m3,ft3)
29.757 0.01
29.623
29.546
28.734
29.641
28.552
29.038
28.699
28.465
28.847
2.431
vs ave stack
ave temp
(C,F)
836.08 85.08
cc
I
GJ
I
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(rain):
Chrg ut
(Ib met):
run
time
Cain)
0
60
120
180
240
300
360
420
480
540
600
605
StEET HOME
RK-18
E5
10-2-89
SH-5G-3B
605.00
16.70
vel dp
(mm H20)
(in.H20)
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
0.042
Units 1-metric,
2=English:
Y, DGM:
Pi tot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.'/. uet):
Burn
stack
temp
(C,F)
93
83
83
83
84
83
83
81
79
80
90
99
(m3
948
978
1008
1038
1068
1099
1129
1159
1189
1219
1250
DGM
rdg
,ft3)
.503
.300
.500
.700
.800
.000
.200
.300
.500
.800
.000
1252.612
DGM
temp
(C,F)
73
93
98
99
99
99
99
98
97
96
96
96
Samp vol
2 (sm3,scf)
1.024 293.351
0.99
28.56 Flou rate
29.5? (dsm3m,dscfm)
0.1963 150.77
18.48
rate (dry kg/hr): 0.61
DGM dH
(mm H20)
(in.H20)
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
vel
(m/min)
(ft/min)
842.14
834.49
834.49
834.49
835.26
834.49
834.49
832.95
831.41
832. 18
839.85
846.70
PR
W>
101.8
100.3
99.4
99.1
99.1
99.2
98.5
98.9
99.7
101.3
105.9
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
29.
29.
28.
28.
28.
28.
28.
28.
29.
29.
2.
std
ft3)
931
239
977
829
925
925
829
977
125
081
515
vs/VmTs
0.01
vs
ave stack
ave temp
836.08
(CSF)
85.08
i
CO
PC
i
OJ
I
NJ
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED (Q - 1 -
DATE RETRIEVED /O "2>
TEST LOCATION |_- <; - OJ ^
SAMPLER SN// "3 V / 6 ~7
<*•=}
-sn
;- Z A^>
WEIGHT GAINS
PROBE 5~..C/
LINE O .9
CONDENSATE 7 / „ S
FILTER// 1 ^Y.tf
FILTER* 2 ^ „ ^
RUN//
TEST TIME 60 S (MIN.) 'i.083 U.'
STOVE ID ft /S -
WOOD SPECIES f7«i
TOTAL (MG)
(HG BAROMETER UNCORRECTED)
PRETEST B.P77.Q (IN HG)
TANK 2Q -- -*?^ (—IN HG) TEMP. 1 / (C)
TORR ABSOLUTE 3rQ
POSTTEST B.P.29. 7T- (IN HG)
WOOD MOISTURE (% DRY)
WOOD MOISTURE (% WET) / S . *"/ Sr
WOOD CONSUMED (LB) [d>C\ (KG) 7. 5 7
SAMPLE FLOW RATE PRETEST
ROTflgETER (^ %" =(ML MIN)
TANK
(—IN HG) TEMP.JL<3 (C)
TORR ABSOLUTE 366 i 3
PRETEST LEAK CHECK
POSTTEST
ROTAMETER
(ML MIN)
START 7, 7.
(IN HSO) FINAL */, g» (IN H20) LEAK RATE
(IN H20 MIN)
POSTTEST LEAK CHECK
START V. 9 (IN H20) FINAL *•/. %" (IN H2) LEAK RATE Q. f (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
co2(i)
02(1)
GRAMS MASS AFTER FLOWING 0.-5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN. +2.6 MIN.
MIN.
MIN,
DELTA
5//-A PROBE+FITTING 3^.
SAMPLE LINE
CONNECTOR
3V.V73/
F-SH-3-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED lo - "L - % l
DATE RETRIEVED
TEST LOCATION £$ - 6
(C)
•5.*?
~?c .7
RUN#
TEST TIME
(MIN.)
STOVE ID
0,^ WOOD SPECIES
WOOD MOISTURE (% DRY) Z-^-fo^
WOOD MOISTURE (7, WET)_L^/g
WOOD CONSUMED (LB) ((?>~J (KG)
SAMPLE FLOW RATE PRETEST
ROTSgETER ^ 9^ = (ML MIN) <
POSTTEST
ROTAMETER d> O
(ML MIN)
PRETEST LEAK CHECK
START y, 5^ (IN H30) FINAL V, y (IN H20) LEAK RATE O. / (IN H20 MIN)
POSTTEST LEAK CHECK
START y.o (IN H20) FINAL I.'? (IN H2) LEAK RATE °>/ (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(%)
RUN COMMENTS:
CO(Z) ?g.
02 (Z)
GRAMS MASS Af-TER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE-HFITT ING
SAMPLE LINE 37 /
-------
CLIENT /rAft
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
•
RUN \Ho.$#~l/ Pf-3$ Placed in Dessicator: Date/Time fo - ? ^
0
STOVE MODEL No. A k-
POSTEST
••
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
)o- V
///*>
}n~-*!o
1 ?^%s>
9-/7-«
FRONT
FTF.TRR It
./77V
.06?
,m
POST WT
. $06 /
. £0£>/
,<,*««
ROOM CONDITIONS
RELATIVE
HUMIDITY
£>^*
y^-^^
V^7,,
BAROMTRC
PRESSURE
Z^-gf
Z^. 75
vt. ?r
Initials
t
X»*"X»
^r/e
/^^
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
GLIEHT
MIL
RUN No. <>/? -
Placed in Dessicator: Date/Time_42^1
<3>it,
ES PROJECT R P /~L!> STOVE MODEL Nc
POSTEST
g
Acetone Lot it . *?// °
Acetone Sample Volume,
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
/ 0- V
*°n%*>
l° wo
9-/ ft. S^
BEAKER il
/9 - %
O,37^T
67- 37 V3
/ -7 o -7 -7 0.060/
r^ oAfl-,
5V? ff^t>c><->
POST WT
iJ O O <5 ^ ^
^ ^ ^ ^ ^ 0 ^—
5-^,^.^
ROOM CONDITIONS
RELATIVE
HUMIDITY
<£> 0^~>o
BAROMTRC
PRESSURE
1?.*Y
H.7S
X9,?y
Initials
»t*4
t
^f.^f
CO
re
i
OJ
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
/'
,n")
(C)
TOTAL PARTICULATE CATCH (A+B+C) =.
4 C''C'-0
6,7
-------
PART ICUL ATE WEIGHTS SUMMARY
Page.
of.
CLIENT
ES PROJECT
3>
RUN No.S/^-l//7/^?/? Placed in Dessicator: nal-.a/Tiine ft) -3
STOVE MODEL No. ^^ V
POSTEST
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
M- 9
H/0
10 - v
n -?,d
/o-sr
n lo
cj,/?-^^
FRONT
PTF-TRR It
5/)£- 33
-/? vx
• l~)3V
c/7/6
" /?/ 6
» /^G<*
£)* o^o^
BACK
FTF.TER It
54£-3
CALIBRATION WT.
WT AMOUNT =
PRE WT
. 4"?9<7
• ^(36 cTr/-O
POST WT
j SCO /
t Sot)/
t 6>'t>f>f>
ROOM CONDITIONS
RELATIVE
HUMIDITY
s*®>t%
yo<3>7a
BAROMTRC
PRESSURE
a
-Z^.VY
T-t?.7<;
-2-7* W
Initials
t
/& «xf
/»i^ /«?
*fc4
I
U)
I
--J
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT ^
ES PROJECT
RUN No. S#-VPJ-^# Placed in Dessicator: Date/Time_/£Ll
D*y//v <^. /o - ~3>
J V ' )
6TOVE MODEL No
POSTEST
Acetone Lot it *)//&.
Acetone Sample Volume
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
(
TARE WT
NET
DATE /TIME
to - v
//3S
lo~ V
OT<
/*-S
/ w^
9- /&'•&*)
RRAKER It
/)-37
•^^.€^77
^^, ^^-^
^*g, , &ao/
^ o . coo ~L
^C) . C> Of if,
POST WT
V3W?
SO'OOO ~l—
$ 6 *(!•&& &
ROOM CONDITIONS
RELATIVE
HUMIDITY
^ @^-%>
vs-^j, v
Qo®7ti
BAROMTRC
PRESSURE
"Z9'SrV
i.?.7S
•z^-gry
Initials
x*ic^
t*tc-4
th^x
I
OO
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTIGULATE CATCH (A+B+C) = I'T-I *S rng.
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page of j
RUN No.$^/'^"3^ Placed in Dessicator: Date/Time_/£Lri!
ES PROJECT
STOVE MODEL No.
POSTEST
Acetone Lot U.
Acetone Sample Volume.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
to- ,a*a-2_
POST WT
i/f,w
x^r^
i
CO
tn
I
U)
I
VO
(BLANK CONG.) x
(ACETONE SAMPLE) - j!
WT GAINED -
O , c
-------
CLIENT
EPA
ES PROJECT RO /"Z-3
P.ARTICULATE WEIGHTS SUMMARY Page of
RUN No. ^M~ £>& ' 3/9 Placed in Dessicator: Date/Time /£>• 3
STOVE MODEL No. ^X- * %
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
1&-. y
It '&T>
/7/5
Ifj - 5"
X"2, / *^
/o -O
q^/7-^
FRONT
FILTER 11
/)*-3/
I. l/o 5
1. // ^^
/.//V7
/./o^J3
.6«5
.-VZ?8
BACK
FILTER 1!
>9*-3t-
.6?39
. 68-37
*/^^
^7tr/
^3 ^>o5S
CALIBRATION WT.
WT AMOUNT =
PRE WT
O£>O
' b&TsO
.^00
ROOM CONDITIONS
RELATIVE
HUMIDITY
Zo<&
vs©>&6<6
BAROMTRC
PRESSURE
^9,<6^
^-9-75
^•<6V
-29,7V
Initials
t
^^
/hC^
/^c^
A^
•n
I
CO
EC
I
OJ
I
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No.5//l^«£il/5_ Placed in Dessicator: Date/Tiine_/^_3_
ES PROJECT fiO Si-
STOVE MODEL No.
POSTEST
to 2.0
Acetone Lot \\
Acetone Sample Volume
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
io~y
ff>- V
-
9-n-W
BEAKER tl
4*.*^*-
6#, 5W0<2-
£*,5o£K
6^^^
O 0 OD'Z t(>
CALIBRATION WT
WT AMOUNT =
PRE WT
$ 6. 660/
Srt *tvT~
POST WT
WW1
$0 060-1.
ROOM CONDITIONS
RELATIVE
HUMIDITY
^ ^ «
V^^S'
BAROMTRC
PRESSURE
Z9.8-V
Z^7^
Initials
W#
m<^£
I
CO
PC
I
OJ
I
(BLANK CONG. ) x
(ACETONE SAMPLE)
WT GAINED
<6(s
Q , O~O
(C)
j O-v
. V^7<^
. o <• - vy
TOTAL PARTICULATE CATCH (A-t-B+C) =_.Vf?Q«6 mg.-
-------
CLIENT
ES PROJECT P f) 12.
P.ARTICULATE WEIGHTS SUMMARY Page. of
RUN No. *>//-$£•"*>/$ Placed in Dessicator: Date/Time lo~
STOVE MODEL No. 4k-/&
POSTEST
WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
•/^-y
//*»
to - V
11 X<7
lo-5
/^//
. 6757
£,tfc-yV
CALIBRATION WT.
WT AMOUNT =
PRE WT
-4"?C>O
, f >&<''<.>
k ^60 ?^
/VlC/J
>,c^
\
/^t c^
PU
I
u>
I
I—•
to
1%
(A)
(B)
- 7
-------
Client __ 'fc_
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run f ' '
ES Project
"Wood Heater Model kl<.-l
Operators CO n n ^
Attempted Burn Rate
TEST RUN INFORMATION
CO Secondary Air Setting
AJ4
Achieved Burn Rate (Kg/hr) .(pj2_ Thermostat Setting _
Primary Air Setting ZQ u^-^^. Other Settings _ |Vj/\
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (X)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
CoTd Draft
Pretest
7&
"2.
Post Test
TEST FUEL DATA
Firebox Volume (ft-)
Coal Bed Range Wt."2^ to
Fuel Charge Range Wt./Z>6? to
i
Actual Fuel Charge Wt
Actual Coal Bed Wt. 3-
Fuel HjOT Dry
Fuel: Dry Kg
Wet
6 . /75
By-pass
Door
Velocity Traverse
p Temp
A 1 636 9^ B
LOADING/TEST START OPERATIONS
Air Settings
Comments
r 6
Ave. p
°K> 2 5,0^S J£_
Pitot Leak Check
Static
F-SH-3-13
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £- />/# Hun It
SH -
Date
- g ^
Wood Heater Model
ES Projec- f /?/? /ZJ5 Operators
Test Fuel Charge
Coal Bed *
Page /'_ of
I
CO
PC
I
10
I
Time
Sampl i ng/
Clock
'02,5
10 '3 S»
IMS
11Z-S
LL
S>" 0
17.00
Test
Fuel
Wt.
(Ibs)
/
0.070
5, C,
0.0^0
5,0
3^
11-1
/2-'<3
IL
Flue
Draft
(in
H?0)
(9.Q1S
ctflo
Comments
1 (, 6 A.
*7 , 'Z
,- \\rt(k*c '«- !
«lso
/-.
Catalyst Temp
FTG (Internal Post
IPO
5' 2.
77 /
Mzz.
7/3
'38 z.
'52
Yf-l
113*}
/i/Z-
78V
^77
lop Rea r Uottom Rignt Left
3SV
(55
/
Surface Temp
5^7
MiL
Z/S"
z/o
/9fi
ZV7
zno
77
^-7V
ZV/
V'/
VZ-7
Z-
Z^Z
/S'7
677
ft'?. 3
SV5
•5*2
$02.
•V/5
2V?
25V
Stack
Temp .
^7
£6%.
III
a 96
1Z^
Oil .
Tun.
Temp .
16-7
^9_
£*«>
^oom.
Temp.
50
So
77
7f
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
'ENGINEERING-SCIENCE, INC.
Client, t Pfl Run I 5//
Date
~ ^ ' 8 *\
ES Projec.
)23
Wood Heater Model
Operators
Test Fuel Charge
Coal Ded
Page 7-^ of
i
C/3
33
I
LO
I
Time
Sampling/
Clock
/*•(/<>
xVzo
/y 3s
xy-So
CO
If* 10
Test
Fuel
Ut.
(Ibs)
9,9
9.
7^7
S.o
lue
Draft
(in
H?0)
.020
Oo2o
.
-------
ENGINEERING-SCIENCE, INC.
Client £PAKun H
Date
ES Projec,
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators
Page
I
CO
33
I
U)
I
Time
Sampl i ng/
Clock
19JQ
^70
2-00")
7.0C/0
IIQO
LI/0
ZKO
Test
Fuel
Wt.
DM
Z.O
fi.DlS
/o
O.S
2.JL
kl
lue
Draft
(in
H?0)
15.01^
0,0(7^.
6.0/6
6.0IO
6,025
o&iz,
0,010
6.0ZS
Comments
7oH
Catalyst Tenp
Pro
VS2-
735
65 /
"Y4
nternal
¥L
Hzc-
/>©&
IH8
Post
37V
fro
Top
^3.
3^7
Surface Temp.
Uear
/a 8
/a?
/as
Bottom
7-73
17 '3
2^7 L
Z-7
26' S
2-77
•2-77
Uight
238
2.3 C,
235
2-3 V
•^•^
7-2-?
218
27 Z
Left
3J7
3 "3
3/9
279
Stack
Temp .
27
Z./3
2^0
22^.
z&L
Oil .
Tun .
Temp
S3
S?
5V
Si
ao
Sb
©0
&0
So
"55"
Room.
Temp.
_?_v_
-------
ENGINEERINGS-SCIENCE, INC.
Client SPA Run »
»/v o OAI A-l/ its,
Date ICs-d-cs ( • Wood Heater Model T "--i O
ES Projec. f
i
en
PC
1
CO
1
t— •
~j
Time
Sampling/
Clock
Z2.3O
2-"£"?> 5
•
Test
Fuel
Wt.
(Ibs)
fli*5
ao
Flue
Draft
(In
H?0)
(?, ft'SO
6,&(fO
,
Kb 12^> Operators
Comments
Zr?& cicx>r op.eAaeP-J-
U^'t, s«— oUj--/ C^ i.*^" K**L^ *\7\t te),tad he fa /<«•
"5^1 •» 0\P$- - St*t0/r*< Lt)r*s>7~
~~J"tf<> /-^OLf) ~ XffT •/
372
Rear
•2-13
Z32_
Bottoni
30 fl
3/2-
Ili ght
ZftS
3ZJ5
Left
<-/i<*
vv/
Stack
Temp .
V7>\
^'^
•
Oil .
Tun.
Temp .
90-
4-?.
i
V
^Z.S
Room.
Temp .
7^
7
-------
j m-'i liLaJLi.'.L
iku^ >i_'-l3?
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater5^v^(7" /-Ic-^i tfJ<-/¥i_
Date
Samf
i / /•. ~*7 ~ O C;
r L) *-~ P /
>ling Location f);^ T—^-^7. /^5-6J5-^
Sample Type ^(S-/~^ <^
Run
Numbe r _s>y '- <5~(C -3/3.
Start Time / ^ •*
Stop Time
l,?_t> Probe Length and
Pi tot Tube Coeffi
Assumed Moisture
Operator /J // /i*?/?
Ambient Temper
Barometric Prt
Static Pressur
Fi Iter Number
ature
js5ure
•e, (Pq)
s)
/ ,C*L, ~?y
^,Z-7v5°
Type /V " cT/>?j$is
c1 ent e 9 9
y%>
Sample Box Number s^ sf-
Meter Box
Meter H
Number
AJ /I
- j i/>
/5
Pretest Leak Rate$,£>/£ n/~ // '/ ' '
Post Test Leak Rated, Mg, , a — ^
(sg (• g / £<7 ~^
Read and Record All Data Every (& Minutes
Clock Time
Sampling (24-hr
time.min Clock)
& 1 2-3O
<& 12 <-zf-"O
2XD /. 2/pO
3<3 /I?CrO
^0 / V0
5° /^>2.<9
&° i^iS)
7" /-z,^/C>
gO ', / So-&
l(c?> J T//O
[70 fc^2c>
/*%> /S~$o
ic£ /•5Vo
^O / ,
i-j° //" ^-/^
t ^^-i^* — S/^i ~^>e—i
Gas Meter
Readi ng
Wn) ft
fc68, 3
/» L3- * -f
fa/Ke/.
(,-L^ -L
t)~$3.-S
^3 %* 6»
(o^'^o 7
o>yft-, ^
^^yL, ^*
(f/^ -6 2_
/>/$/« V
6<^7^ 6
<^7V. 7
6T?. ^
^} (5 y f* ^-—
£* "?
y ~^^ • ^B.
Velocity
Head
( PS). in-
H?0
fi'.C'V 2-
V -t^
> oty 1
,.0^1-,
fo V"2—
•« <3^/ 2.
» So
, & £•
' SO
• ^ C>
i. ^ D
< X" O
w SO
» % o
ff <%c>
it { ~) CJ
„ ^ 0
i ?> 6>
> 5^ £?
„ S' ^>
« ^f <^
£, ^ O
, So
- So
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
^7 *"/ "
~1 (-(•
%0
5"^-
^ S"
3 7
87-
87
9/
9/
^,'3
9^ -
Cfc/
94,
9^
9y
95 -
95
q 5
*^ *5
^
I ^i± — 1
Filter
"70
76
•
Implnger
(JcV
fT /
6- 9 <5'1.
69 '5-7-
7 o
5 1
69 ^^
7o ^y
7^> ^V
76
5*/
5 *7
"/ fj 3 .S
/ £? ^" ^*
?<5 5"i.
TA ^_Li
10 t,t
7c? I C
"?{> 77
7^> <5 7
7 / ^5^
-7o *T5?
7^> 5"^S"
-^s %§-
— Z-S^ ^-^ 1
Pump
Vacuum
1n. Hg
~>
•7_
2
•?
2_
•2L-
7
"2_x
•2__
2
< — ^
T_
~Ls
z__
"2_
~z_
~2
"r^
2-
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
- 2. ~
Sampling Location £~jf -
Sample Type -2. ft /
Run Number <^& -
.Operator
//
<=/ P
r ?
Cl
Sampl ing
time, min
ock Time
24-hr
lock)
Gas Mater
Reading
) ft3
'
Velocity
Head
(&PS) in.
Orifice Pressure
Di fferential
(AH).-in. H?0
Desired
Actual
.Bo
TEMPERATURES
Dilution
Tunnel
Meter
In
Meter
Out
Filter
70
Impinger
Pump
Vacuum
in. H g
Flue Draft
in. H?0
3J.
2,7 o
7V A ST
0 ,
2S2*^0_
nfO
•72-
6V
0 .
-------
SAMPLING DATA (cont.)
Vlood Heater
Tl
I
V)
PC
I
CO
I
ENGINEERING-SCIENCE, INC.
Date /O-Z-B>5
Sampl i
Sampl e
•> -j
ng Location D>"1 "^~C_
Type
^"50-
Run Number ^i-A - "56- ~ 3/4 — /—
Operator |^ y\ Q /*/ -2
•
\. Clock Time
Sampl ing\(24-hr
time, min\£lock)
' — —
^v) T.G Oe?
t-fCjo 2° "Vo
S?-e> ">< 1 O
5" 3o ^J ^o
5^0 -2170
^0 "2/VO
S'oO '2/*>o>
5 7 o Z'2^0
5Qo ~2-"7.to
^^O ~2-*2,~Z£>
{fQ($ "2-2-3O
^Cr3 2-Z'3^
^,0^
Gas Meter
Readi nq
(!tn) ft
&V7..S
B5Z- C7
8S7' Y
R6 Z. "^.
^6?. 1
87^0
Pi77, -*>
ea?. ?
©9 z. '"b>
Q*i "7 1 <-/
*?o "2 . v
7o 7«S
•fe"
cj/d^y^
3o^.737
Vel oci ty
Head
£>O<-/ 2.
0-07 7,
O.CX/'L
O.cJVi-
£>-O<1~~l.
A-dy "2_
O-CC/^
6-0^1-
<5iOV2_
Q.O-/T_
6-Ot-fi_
<5'°Y"Z_
ft
tOy?-,
Orifice Pressure
Differential
(AH), -in.
Desi red
H20
Actual
•So
. & o
iSo
•So
-&c)
t c^O
^So
V ($'CJ
t £>o
i "80
i<3 o
i c£>c
/&o
, g£>
TEMPERATURES
Di lution
Tunnel
.
1
V
*Sl ,^
Meter
In
-
Meter
Out
*"! 1 ~
^ 1
9/
7/
c ^ y
I/
¥/
' /
*?/
9 /
*?/
"T/ -
°j Ik 1
Filter
<£> c(
C6 ^
^1
69
6?f
6.-^
4 ^
G 9
^0?
^ ?
57
67
Impjnger
^G?
S^Co
^GP
^"7
^~? •
57
^•~?
f^Oj
<$ Pj
1?S
5-9-
55?
^7
-
Pump
Vacuum
in. Hg
Z.
2
~2-
-f
^>
£
~^>
^
2_
^>
"2_
2_
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater Si^p^y Her**? ^AV?
Date /& - 2. - % 1
Sampling Location £) S£ cff/cr-i. -^Z. J^S-tdS-t^b
Sample Type 5
Run
>& / 7 5^
. .
C'' X
Start Time I ^ ^ °
Stop Time
Probe Length and
z,^^^
Type /^/ '' /*-.
Operator i£>j-j fac-ft "
Ambient Temperature
Barometric Pn
Static Pressur
Filter Number
Meter /, o z
jssare
Ke, (P.;)
s)
-V
Assumed Moisture
ty
Sample Box Number
Meter Box Number
SJA'o9 ^Q// /7
Post Test Leak Rate • <5,<5G/ ^. // /^
Read and Record All Data Every '^ Minutes
Clock Time
Sampling (24-hr
time.min Clock)
1° l~2,^^
~Z-° / 7^>O
3-0 /"&oo
t-tO /^\/o
SO f'S'Z-0
&>£> rvi&
7o J-2YO
Q£ A/oo
le^> /L//o
\(O / /yy^
/t/O yyTtJ
(£c /^^
/t£ / 9/o
f ?£> y ^T ^ o
{90 / 5" ^o
/^<) . j^tyo
7 co / ^^d
1\& / 6 &d
11D /(~> lO
2,-j0 ifatO
nW t/h-^o
Gas Meter
Reading
(vm) ft3
9«53 , f-t
*•?*•>%» ~\
&(a ? • •?
9<£ ^i ^
•973«y
£) -~\ C^ "?
9^ 5"
)a>~*>t5
jot^i-S
//>23 1 _5"
/(9'Z ?T (i'
/V~Z-
* o Vt_
.* ^VZ,
- ^vz.
«<^^2_
*OVL.
t O *-/ T-.
,&y"L
, o>-/Z-
,6<-/ T__
,6^ T_
.cW2_
Orifice F
Differe
( H), in
Desired
,^«=,
i ^t>
'ressure
:ntial
H20
Actual
1*15
j •> ^
-95
«• ^
5<7
"77 5"^
7,7 • 5' <:
77 5"^
7~? "T7
77
53-
77 5-^
77 ,T9
77
5-7
77 ^^3
Pump
Vacuum
in. Hg
^j,
IrS
^3
•^
jg
T
1
j?
7
^
^?
_^
•?
3
3
"^
"3
"?
3
3
J3,
"^
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date /a-',
Sampling Location £5 -
Sample Type ~2 %/ <;c-
Run Number
,S//-'
Operator U) ^ -
l>
Clock Time
S amp ling\(2 4-hr
time, min^x£lock)
Gas Meter
Readi ng
1U
Velocity
Head
UPS) in
C-CW 7
Ori f ice Pressure
Differential
(AH), -in. H?0
Desired Actual
TEMPERATURES
Dilution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. HgO
77
_£.
J22.
^L
/720
. £3 V-?_
l£
> v "
-
79
-^7-
^77
TV
O.OH 2-
^2.
"77
370
f •
7?
, ?_
6
_^JL
^Z-
Ce.6
AQY ?
•7*=;
f 6 -
0. 0 L/ T,
-^X
? a
0.
Li5_
ZfzL
o
7V
-------
SAMPLING DATA (cont.)
Wood Heater
ENGINEERING-SCIENCE, INC.
- Date fC>-7. -^H
Sampling Location \5T~^ 1_
Sample Type
f-\c^6—
Run Number ^SV4 — c;6-^^~^
Operator VA^ U <-> /
i
C/l
pfi
1
OJ
1
• \^ Clock Time
SamplingX^A-hr
time, min\£lock)
" ' • — — — _
*l& 0 "2o.3C>
£/ 2£*> &
"7/O -^.toO
^IJO ~L* 10
^3O ~U 2-0
Si to 2-1 ~So
*?$o ~2A ^O
*7(aC)_ '2-1 *a«i>
*o7G '2-Z^o
SS'o 2-Z'C>
«^"?0 "2-220
A CO 2-Z3O
^0^ ZZ3S
CoO G
Gas Meter
Reading.
(vn) ft3
//fe1?. S
// 7Y-Q
//99i "7
1*2.0^ <^i
}"ZO "7. C>
j'T,/ .c"Y -z,
Oe.o«-r?
o. O'YT,
D-OV^-
(?..CCY -T_
CcO'-/-z,
0iO«yz-
O. o«YZ-
O.QtY' "£_
0-0*72-.
Q.nQl-
Orifice Pressure
Di fferential
(AH), -in. H?0
Desi red
Actual
i 9 *5
• *? S
. 7^
t7 5
' ^x
. 9 s
4*7 <;
t ^S
/*? *^
.75
.fS
•^^
» 7*S
. q 6
TEMPERATURES
Di lution
Tunnel
•
/
V
'SZ/V
Meter
In
-
Meter
Out
t?7 -
<7 -7
?~7
? 7
?7
76
?6
?"Cf3
7-?
~7^T
Impinger
Co ~\
& ~L
(6 *-/ '
fc5"
tf 5
ci 5
65
5V
5-7
T<5
•
Pump
Vacuum
in. Hg
"^
~^
-^
'N
-^
•^
-^
3
-^
-^
"7
Flue Draft
in. H?0
CJ
-------
FUEL MEASUREMENTS
Date /(> -rL~ Mood Heater Manufacturer
Project No. C,^ 12,3> Wood" Heater Model
Run No.
Circle One: (^Tjretes_i-FtJe1 Test Fuel
Fuel Type and Amount 2x4 ^/ 4x4 1x4
Ideal Load Weight ; .Actual Load Weight ~_
Fuel Piece Length
-------
FUEL MEASUREMENTS
Date /£-c-
Project No. g fs,
Run No. .Sft-:V
Hood Heater Manufacturer
Wood" Heater Model
Circle One: Pretest Fuel *fest Fue!P
Fuel Type .and Amount 2x4 2_ 4x4 TL- 1x4
Ideal Load Weight '
.Actual Load Weight
Fuel Piece Length
t~7
Moisture Meter Calibration .12%
KA.C J T< «, O. °F 'TT- • ~
}
225
"2.
Piece No.
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)- Corpse Ted.
Readings Average
2M
z/S
tfn
ri
Overall Fuel Moisture Average
F-SH-3-25
-------
TEST
SH-4
WS\RD123.40
RJM1381AAPP
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: SWEET HOME Units l^metric,
Model no: flK-18 2=English:
Lab name: ES Y, D6M:
1st date: 10-3-89 Pitot co:
Run no : SH-SGHfl Gas MW :
Tst time Pb (mm, in. Hg):
. (min): 540.00 Stack area (m2,ft2):
Chrg ut Wood moist (.?. uet):
(lb uet): 13.90 Burn
run
time
(min)
0
60
120
180
240
300
360
420
480
540
vel
(mm
dp
H20)
(in.H20)
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
041
041
041
041
041
041
041
041
041
041
stack
temp
(C,F)
103
105
106
108
105
101
107
102
99
100
DGM
rdg
(m3,ft3)
53.036
83.500
114.100
144.400
174.500
204.800
235.000
265. 100
295.000
325. 132
DGM
temp
(C,F)
94
99
102
102
102
102
101
99
95
94
Samp vol
2 (sm3,scf)
1.00? 257.408
0.99
28.56 Flow rate
29.74 (dsmSm.dscfm)
0.1963 146.92
18.33
rate (dry kg/hr): 1.81
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
vel
(m/min)
(ft/mi n)
837. 14
838.63
839.37
840.85
838.63
835.65
840.11
836.40
834.16
834.91
PR
(2)
102.1
101.6
100.3
99.0
99.2
100.3
98.7
98.3
100.2
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
29.
28.
28.
28.
28.
28.
28.
28.
28.
std
ft3)
107
976
539
350
539
444
401
313
738
vs/VmTs
0.01
vs
ave stack
ave temp
837.58
(C,F)
103.60
a
i
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
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
120
480
540
SWEET HOME
RK-18
ES
10-3-89
SH-5G-4B
540.00
43.90
vel dp
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
041
041
041
041
041
041
041
041
041
041
Units l=metric,
2-English:
Y, DGM:
Pitot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.?. uet):
Burn
stack
temp
(C,F)
103
105
106
108
105
101
107
102
99
100
DGM
rdg
(m3,ft3)
253.028
283.200
313.600
343.800
373.800
403.800
434.000
464.000
494.200
524.417
DGM
temp
(C,F)
75
96
102
103
103
103
103
102
100
97
Samp vol
2 (sm3,scf)
1.024 261.697
0.99
28.56 Flou rate
29.74 (dsm3m,dscfm)
0.1963 146.92
18.33
rate (dry kg/hr): L81
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/mi n)
837. 14
838.63
839.37
840.85
838.63
835.65
840.11
836.40
834. 16
834.91
PR
tt)
104.8
101.6
100.1
98.5
98.1
100.2
98.1
98.8
99.7
dDGM
vol std
(m3,ft3)
30.367
29.441
28.935
28.693
28.693
28.884
28.693
28.935
29.055
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
837.58
(C,F)
103.60
PC
I
-p-
I
ro
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED /£ - ?- g"5
DATE RETRIEVED
TEST LOCATION
SAMPLER SN#
PROBE
LINE
CONDENSATE
FILTER#1
FILTER//2
RUE* SA> ~ (JPJ -
TEST TIME
STOVE ID
(MIN.)
"2-
(HG BAROMETER UNCORRECTED)
PRETEST B.P79.fr9 CONNECTOR *
MIN.
MIN.
MIN
3V. <
?. V, A? 20
DELTA
F-SH-4-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED /a - 3- 3
DATE RETRIEVED
TEST LOCATION bS-tJ
SAMPLER SN# /0 (IN HG)
TANK "2- 9'
TOTAL (MG) 5 a 5
^tfit ,
DRY) ZZ^
("IN HG) TEMP. 1 X (C)
TORR ABSOLUTE 6-O
POSTTEST B.P. '7.(-J,aiO (IN HG)
TANK ^,^-^~ (--IN HG) TEMP.7^ S (C)
TORR ABSOLUTE 3 3 1 ' "5
PRETEST LEAK' CHECK
START
(IN HSO) FINAL;
H20) LEAK RATE -£-.
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
*
RUN \Ka.S#*UPT-yQ Placed in Dessicator: Date/TimejIcL^L
ES
STOVE MODEL No.
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
16 -H
IV /a
ic-<;
)•*>/&
9-/7- "8?
FRONT
FILTER It
54^^n
* iin
• fltS
0 • ooo'L_
CALIBRATION WT.
WT AMOUNT =
PRE WT
. 5^00 0
« *> 00 /
POST WT
. Vf9S
» ^ &a&
ROOM CONDITIONS
RELATIVE
HUMIDITY
V5©J^
Vo ^7..
-
BAROMTRC
PRESSURE
•z?-75
29-Sy
Initials
i
y^iC^
A^ /?
33
I
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT k
ES PROJECT
RUN No.<9//-//A7'-V/t? Placed in Dassicator: Dat.e/Tiine
S'TOVE MODEL NO.
POSTEST
Acetone Lot it
Acetone Sample Volume
<£
//
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE/TIME
/0-ST
n^^
id -&
/G0&
9-/s-^
BEAKER It
/9 - V/
7o,3/6£
7^- 3/r; •?
9£? , 3/6 3
7o. 3o9Y
a c o*> 6 9
CALIBRATION WT
WT AMOUNT -
PRE WT
*-) O , isoC'O
S"<3 . £>£>
POST WT
Zo.&eoo
5 'A, oo&O
ROOM CONDITIONS,
RELATIVE
HUMIDITY
VO&70
V&6*
-
BAROMTRC
PRESSURE
•z^.sy
^9,7y
Initials
/^r ^^
syi^j^
i
CO
re
(BLANK CONG. ) x
(ACETONE SAMPLE)
WT GAINED
o
(C)
2-
TOTAL PARTICULATE CATCH (A+B+C) =.
9»
-------
CLIENT
ES PROJECT RO'/£.
PARTICULATE WEIGHTS SUMMARY Page of
•
RUN No-S/V-^/X-V^ Placed in Dessicator: Date/Time./!:
STOVE MODEL N
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
,WT GAINED
DATE /TIME
to - V
/« ^
/o-r
/•^ /Vj
7-/7-S9
FRONT
FILTER it
S46-V/
- /i/6
tlT-il
• /T-/-7
•»/2o'B
O o 000C\
BACK
FILTER tt
5>9d-V"2-
*/1.o/
« /^./
i *)Crrj'Z.
POST WT
, V9??
«> $&t>o
ROOM CONDITIONS
RELATIVE
HUMIDITY
^@^«
Vo^-7^
BAROMTRC
PRESSURE
z 7.75-
•Z9* ^5V
Initials
l
fri^tf
factf
I
C/5
(A)
.(B)
i
— i
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page
RUN No.$//~lJPj- V/3 Placed in Dessicator:
of.
ES PROJECT AD
L/
CALIBRATION WT
WT AMOUNT =
PRE WT
50,00*0
5&.&06Q
POST WT
^o.oco*
5 o.o^o
ROOM CONDITIONS
RELATIVE
HUMIDITY
Vo®7-o. '
Vb©^
BAROMTRC
PRESSURE
19 -vr
z^- 7y
Initials
/^^/e
a
I
IX
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
r>
(C)
TOTAL PARTICULATE CATCH (A+B+C) =.
. S
9
rng.
-------
CLIENT
ES PROJECT ftP
PARTICULATE WEIGHTS SUMMARY Page of.
RUN No.9/^-9^" V-*? Placed in Dessicator: Date/Time.
STOVE MODEL No. A K-J *&
POSTEST
Acetone Lot . ..
Sample Volume V i
/'
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
i.
TARE WT
NET
DATE /TIME
lo-S
'*6So
9-eo~?>?
BEAKER' It
/?-V2>
£?.//>47
6 *? . if? y <&
^9/ / (t> t/'%
60 / c: *z £^
V , f > o O
^ n O 0 6 "^
CALIBRATION WT
WT AMOUNT =
PRE WT
<}0f<«*c.
$0.0*00
POST WT
^ Q j (?& (* £^
^ ^1 , &&& O
ROOM CONDITIONS
RELATIVE
HUMIDITY
fy&io
V<&>6*
BAROMTRC
PRESSURE
-£.
-------
Page.
of
CLIENT I
ES PROJECT
D
PARTICIPATE WEIGHTS SUMMARY
RUN No. £^£6-- V>9 Placed in Desslcator: Date /T i me 7/0 - V & Wot,
STOVE MODEL No. /) K- J *¥
POSTEST
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
\o- V
IV c.^
1Q-S
l-Z-7.0
9^/7-^9
FRONT
KILTER If
/kf-3
BACK
RTF.TRR It
/) ^f- Vo
•6^ol
• (P^
.Wl
6G>7(00
6*o^°(
CALIBRATION WT.
WT AMOUNT =
PRE WT
» ^oO Z_
> $<:'« ~L.
POST WT
.VfCyf
i
i
i—1
o
(A)
(B)
-------
,CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY ' Page of
RUN No. <>#-<;6-- V/3 Placed in Dessicator: Date/Time_/£.
/"Z-3 STOVE MODEL No. /) K -
POSTEST
Acetone Lot it
Acetone Sample Volume__Z_2_
/V5"
WT 1
WT 2
WT 3
WT 4 '
WT 5 '
FINAL WT
1
TARE WT
NET
DATE /TIME
/*-5
/ -3
/£-£
y/9 //^
. •
9-/S-S*?
BEAKER 1t
/?- vy
7^ >H57S
7o. ^7
CALIBRATION WT
WT AMOUNT =
PRE WT
5~£>/ OO6O
*-) CJ . &&£>£*
POST WT
^O'&C>OO
*>t>.600f>
ROOM CONDITIONS
RELATIVE
HUMIDITY
y^ ?o.
^«^T
BAROMTRC
PRESSURE
-Z9 .W
Z <)'?
-------
PARTICULATE WEIGHTS SUMMARY
Page
of
CLIENT
ES PROJECT A D /Z3
RUN No.5//-56--V/3 Placed in Dessicator: Date /Time
STOVE MODEL No. £* K
POSTEST
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
lo-'i
/ ^ ^5
A»-5T
i~i.-T-.fj
9-/7-S?
FRONT
FILTER It
/9/f-V/
„ -77. ^V
.72^3
- 7 29 3
«6«3?r
^oOV^S
BACK
FILTER II
/?£- V7-
-6%V7
* /f^V.^
*6^y^
,~L,
f "} ' a-o Z,
POST WT
,y??9
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run /
ES Project ? \ h /
'Wood Heater Model
CO $(l
Operators
Attempted Burn Rate
TEST RUN INFORMATION
Secondary Air Setting
Achieved Burn Rate (Kg/hr) //8V; 7 Thermostat Setting.
Primary Air Setting rt0^ _ Other Settings f\lA-
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%}
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
VS'/,
Post Test
TEST FUEL DATA
Firebox Volume (ft-)
Fuel Charge Range Wt.
Actual Fuel Charge
. 6 to .
Coal Bed Range Wt. 2,6 to 3-.
Actual Coal Bed Wt. "S-0
3% Dry *22 ///Wet
Fuel: Dry Kg / 6 <• Z
• LOADING/TEST START OPERATIONS
By-pass See|- Air Settings
Door n&^2gj/ (^ Q; ITX. Comments
Velocity Traverse
Ave.
Pitot Leak Check
Static
F-SH-4-13
-------
ENGINEERING-SCIENCE, INC.
Client fcVA. Run If
Date
ES Projec, It
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Oed
Wood Heater Model
Operators
Page
/ or 3
w
i
4>
I
H-'
4>
Time
Sampl i ng/
Clock
/30
/Zoo
zfcb
Test
Fuel
Wt.
(Ibs)
Ho
v/s
3.R
L3-
6.5
I.T
Flue
Draft
(In
H?0)
b.c^O
6,470
0,44,5
C,D(ot.
Comments
'ftll
UUg
Hoy r/1
Catalyst Temp
R (Internal
tn&
(12T-
LL12.
LL22,
il\t
ins
/27/
/I 3*7
\\i~-~i
Post
tool
!?$(
usi.
/C/.Q
IOZ3
Tp""~"
Top
(bOQ
5-70
6/7
57
Rear
Surface Temp.
7
3VS
Hot torn
Z.33
77V
yzS
EL
Y£6_
V6/
Left
59y
703
5VS
sv/
67 b
-7/3
Stack
Temp.
5"S"^
Oil .
Tun.
Temp.
102.
^oom
Tem
:z_v_
j£L
2.SL
-76"
7*9
7V
7?
so
-------
ENGINEERING-SCIENCE, INC.
Client ._&J3Q Run f
Date
ES Projec,
WOOD HEATEH CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Wood Heater Model
Operators
Page C
8 Coal Oed
Time
Sampl i ng/
Clock
EC
I
*-
I
i—>
en
"/3o
/Wo
<5 In
00
Test
Fuel
Wt.
(Ibs)
6,0
3, -5
0,0
IZ.3
/0,7
a
Flue
Draft
(In
H?0)
0,0-70
0,070
tf'L'C
O.O6O
^.070
^070
AOJO
6,6-jO
Comments
Catalyst Temp
Pre
~K~L
213
1/2.1
935".
'ISf'J
tor]
nterna
M35
•V99
I1
A. 7V
in /
Post
95"^
85ft
//fit/
liiz
"IS
Top
VW
56S
5-/V
$0%
6/6
56, f
Surface Temp.
Itear
•35 /
32-7
31
•503
3TZ.
llottom
•3
337
335
330
-731
339
•3-v/
•3.
Kight
V99
Left
65 -
5VO
41/0
5'70
5-50
-It±
Stack
Temp .
5S7
VC7.
on.
Tun.
Temp .
/Cl'l
/oft
Job
/o^
/A 7
/OS
' O '—7
/03
Room.
Temp.
(5s "2-
83
-------
ENGINEERINGjiSCIENCE, INC.
Client ^f/V Run g
Date
ES Projec,
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ued
Wood Heater Model
Operators l
Page JS of 3
Time
Sampling/
Clock
i
CO
PC
I
/Slo
ifevc
/85o
i u
Test
Fuel
Wt.
(Ibs)
2.0
1,5
, Z_
6. 0
Flue
Draft
(in
H?0)
0,060
CvOi.0
Comments
ft.
7. - T-
0. c -
Catalyst Temp
'Pro llnternallPost
7Z3
/a1?1?
/£??
37S
3-7 /
360
Vr
bottom
"^20
2l±.
33o
SS
Right
Left
6VV
61-1
-------
El .'.I., i ^
HC;<=- Pi tot Tube Coefficient ,^^7 \
Number SM -^(^ <^//
Assumed Moisture <-,/
Operator \yit^VA A >vOS
Ambient temper
Barometric Pr<
Static Pressur
Filter Numben
Meter V
^ature '
;ssure
•e, (P.)
s)
Sample Box Number
Meter Box
Meter H
Number /> S - ~^,
Pretest Leak Rate 6,0 1 S <^'''
/4 e / "TC" "}
Read and Record All Data Every /O Minutes / • ° — '
Clock Time
Sampling (24-hr
time.min Clock)
5 ||T-£>
/D \}~^>&
Zo \IH£>
•^G i /c;o
^o / ?.ot>
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7o / 7 T O
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J^O ("?-/£>
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f&-> fc/^.(^>
( 1& N')<3
2&o / LJ^ /f^o
7-20 f<5&<3
7-^0 r-*>t&
2^"/o /3'7c3
Gas Meter
Reading
(vm) ft3
06 3.£k3
Sfe.G
63,0
•73. /
~)fte 3
8^ . S>
3^t Qp
?"? . ~7
9'fe • R
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left-/,!—/
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Velocity
Head
( PS), ^.
H20
6-CH/
O.OM/
O'^^n
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<*>,&'-//
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d^o^y /
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6.0--//
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Orifice r
Djffere
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Desired
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4 ^5 ^
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, £bo
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-so
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• . % o
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jntial
H20
Actual
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ao
' "&&
' <$£>
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• SO
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TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
<^Y_
C/S
96
°t 7
v #
9' 9
9-7-
/o6
/oo
(&(
/o/
/o/
/"O2_^
/6 Z,
/"O> ;?
/02^
/07,
/dJ '2 -
^0 i_
/^ "2.
/O~L~
/O 2-
/^ 'Z-
7^2,-
Filter Impinjer
7i / 5~o
S"^ V(£.)
« 3 f 7
5 5"-^
g<; 5"^
©5 S" ^2>
SSL 5' 3
f?S 5 3
r%;r> S*V
S 7 5 <-/
S-? -y-s
^^ 5'S
¥ Si 5
<*-? <56
-6?
Pump
Vacuum
in. Hg
~i_
^_
~^>
~2_^
•2.
7
c"
^
"2.
^
^>
2^
-$_
-^
z_
~>_
'2_
"2.
"2^
7.
2.
~2_
?-
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date ^ /
Sampling Location £5--
Sample Type
Run Number
Operator /
- V/?
c
Clock Time
S amp lingXJ 24-hr
time, min^vClock)
•2,66
Gas Meter
Reading
(Vm) ft3
y* o
Velocity
Head
UPS) in.
0
Ori f ice Pressure
Differential
(AH), -in. H?0
Desi red
S'o
Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
7_
Filter
5
Impinger
5S"
3ump
Vacuum
in. Hg
Flue Draft
in. H?Q
7
V/
, 0
-z So
J-
i SO
So
av
. a
1 80
.6*0
.So
• So
/6
as
So
/oz.
S'S
-So
©0
/o/
/o /
ftoi
2-50.
. so
•Ss
2-
,80
'80
a.
>0 . 0
^£°
v?
i
CO
I
I
H-1
CO
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
Sampling Location_
Sample Type_
Run Number
Operator
\Clock Time
Sampling\(24-hr
time, min\Clock)
""• • • ____
VAo /^2-
5/£?c>
530 ^ClCi
S^/0 "2020
5<-//
^c^'y/
.04^ ^
*.&H(
&/(
f0^/
cOCVf
«c»V/
Orifice Pressure
Di fferential
(AH), -in. H?0
Desi red
. §^O
. §>o
. &&
,&o
,80
.ao
t ^)0
Actual
. So
« S>o
-ao
^-<6
. 8r>
'So
,So
.^0
TEMPERATURES
Dilution
Tunnel
I.
V
/* '
fcy
^V
73
2V
?V-
99.5
-
Filter
So
Bo
7<7
7S
75
-78
7A
Impinger
^•^>
f??
5Q-
5"
2-
-2_
•*_
Flue Draft
in. H?0
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number^
Operator
,
**
Start Time
Stop Time
//
Ambient Temperature
Barometric Pressure
Static Pressure, (P^
Filter Number(s)
Meter
Probe Length and Type_
Pitot Tube Coefficient_
Assumed Moisture
Sample Box Number
Meter Box Number
Meter H
- /
Pretest Leak Rate fl,Qo,^
Post Test Leak Rate 61004.
11
l\'t
~- (• o Z- *-/
Read and Record All Data Every
Minutes
Clock Time
(24-hr
Clock)
Vel oci ty
Head
( Ps). in-
Sampling
time.min
Gas Meter
Reading
ft
Orifice Pressure
Di f ferential
( H), in. H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue
in.
Draft
H90
O
2.0
ZS3.0Z&
76-
251
-7B.
0
Q-
s
/
5-
.3
O
95-
Z2_
-&Z
7LJ( O
8
>O
95
O
V /
2
rs
-------
K2H3J
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood Heater
Date jg-
Sampling Location £ <,-
Sample Type
Run Number_
Operator
S#~
Clock Time
Sampl ingX^A-hr
time, min\£lock)
Gas Mater
Reading
lYJjLtL
378.
Velocity
Head
(APS) in
H90
Ori fice Pressure
Di f ferential
(AH), -in. H?0
Desired
Actual
-------
rpHsa^piEi
b.r-.Tn PT-—m-«.
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater
Date
fo-
Sampling Location
Sample Type
Run Number
Operator
^\ Clock Time
Sampli ng\(24-hr
time, min\£1ock)
* ' " — — — — -~
o /9^-/o'
f9/ ° /9s' o
5"i?o ZX^DO
^'3<^ 2^>'^
^VO Zo z o
^o
Gas Mater
Reading
(vm) ft3
^/9V, t.
V99. -L.
^•o^,^
$/$>.?>
fj/*?. W
^2,H^n
•2.7/,3V
??
^
^6
97
f-7-
33J*-
Filter
&-\-
&~\
8^
c5^
a?
»/
a/
Impinger
G /
«V
<^r.
c^'^
67
6-*
£S
•
Pump
Vacuum
in, Hg
^
"^
^
r\
^
^
•^
Flue Draft
in. H?0
EB
I
I
10
to
-------
FUEL MEASUREMENTS
Date
Wood Heater Manufacturer
Project No. i^j^ /Z.
Run No. ^tf - y
Circle One:
Fuel Type and Amount
Ideal Load Weight
Fuel Piece Length
^.
> — r "^
Ptetest_Euel
2x4 <•
. nj (&"
Moisture Meter Calibration 12%
\fJoe-rl T*»,p. °>- *7,
' t
Wood" Heater Model frl.- -/ •>*
.. Test Fuel
-^^ 4x4 1x4
.Actual Load Weight
/ 7_ 22% 2_Z_
.
Piece No.
1 ^T
2
3
4 •
5
6
7
8
9
10
11
.12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Readings ' Average
Overall Fuel Moisture Average
F-SH-4-23
-------
FUEL MEASUREMENTS
Date
Project No.
Run No.
Wood Heater Manufacturer ScOeW""
Woo
Circle One: Pretest Fuel
Fuel Type and Amount 2x4 <-— 4x4
Ideal Load Weight
Fuel Piece Length ;~7
Actual Load Weight
Moisture Meter Calibration 12%_
221.
Overall Fuel Moisture Average /3»7
F-SH-4-24
-------
TEST
SH-5
W5\ilDU3.40
WM1381AAPP
-------
Hpthod 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(rain):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
210
300
360
120
180
510
600
617
SWEET HOME
flK-18
ES
10-1-89
SH-5G-5H
617.00
52.10
vel dp
(mm H20)
(in.H20)
0.011
0.011
0.011
0.011
0.011
0.011
0.011
0.011
0.011
0.011
0.011
0.011
Units l^metric,
2=Engl ish:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (2 uet):
Burn
stack
temp
(C,F)
90
95
91
100
97
91
100
96
102
102
99
97
DGM
rdg
(m3,ft3)
326. 105
356. 100
386.100
116.500
116.100
176.600
506.600
536.500
566.100
596.700
627.000
636.605
DGM
temp
(C,F)
68
87
90
90
91
92
92
91
93
96
97
97
Samp vol
2 (sm3,scf)
1.007 299.991
0.99
28.56 Flou rate
29.81 (dsm3m,dscfm)
0.1963 117.91
18.31
rate (dry kg/hr): 1.88
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
800
800
800
800
800
800
800
800
800
800
800
800
vel
(m/min)
(ft/min)
826.15
830. 19
829.15
833.93
831.69
829.15
833.93
830.91
835.11
835.11
833. 18
831.69
PR
(2)
103.
100.
100.
98.
99.
99.
98.
99.
100.
99.
110.
6
1
3
6
I
6
1
7
1
0
5
dDGM
vol std
(m3,ft3)
30. 111
29.390
29.037
28.811
29.080
28.836
28.739
28.792
29.071
28.911
9.119
85.19
17.610
160.00
1850.00
vs/VmTs
•
.00
vs ave stack
ave temp
(C.F)
831.81 97.17
I
CO
PC
I
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
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
-120
•180
540
600
617
SHEET HOME
RK-18
ES
10-4-89
SH-56-5B
617.00
52.10
VQ! dp
(mm H20)
(in.H20)
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
Units l^metric,
2=English:
Y, D6M:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.7. uet):
Burn
stack
temp
(C,F)
90
95
94
100
97
94
100
96
102
102
99
97
DGM
rdg
(m3,ft3)
525.800
555.600
585.800
615.800
645.800
675.700
705.700
735.700
765.800
796. 100
826.400
834.959
DGM
temp
(C.F)
67
89
93
95
95
96
96
96
96
99
99
99
Samp vol
2 (sm3,scf)
1.024 302.138
0.99
28.56 Flou rate
29.81 (dsm3m,dscfffl)
0.1963 147.94
18.31
rate (dry kg/hr): 1.88
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
826.45
830.19
829.45
833.93
831.69
829.45
833.93
830.94
835.41
835.41
833. 18
831.69
PR
(Y.)
104.1
100.7
100.4
99.0
98.4
99.9
98.7
100.4
100.5
99.5
99.1
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
30.
29.
29.
29.
29.
29.
29.
29.
29.
29.
8.
std
ft3)
520
690
280
175
077
122
122
219
413
256
264
vs/VmTs
.00
vs ave stack
ave temp
831.81
(C,F)
97.17
I
•si
S
I
j\
I
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
'
DATE DEPLOYED
/6 -
UNCORRECTED)
^ftf (IN HG)
(—IN HG)
•2,.?
~ip.*<; (IN
(—IN HG)
-3<73.7
WEIGHT GAINS
PROBE — 2 . *%
LINE - £ _ <%
CONDENSATE /?. "?
J_- FILTERS! -2,y
FILTER//2 -+ £>t£f
TOTAL (MG) V/ 7
TEMP.'ZpfC(C)
HG)
TEMP. "Z_/ (C)
Itbl liilr. Lg
STOVE ID fik
WOOD SPECIES^
WOOD MOISTURE
WUOD MOIbTURE
WOOD CONSUMED
11 (MIN.) /0.2-S3'
-/^
^tv^ /^-5 /T/>^
(% DR^) Z2'VZ-
(% WET) fS-!> 1
(LB) 5"^- 1 (KG)£3.
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
,-y.S'
DATE DEPLOYED (O - V - % 9
DATE RETRIEVED
TEST LOCATION£"S-k?S-^*£
SAMPLER SN// ^ 0 / $ <;
(HG BAROMETER UNCORRECTED)
PRETEST B.P^Cj q/ (IN HG)
TANK "2. 9? «0 (—IN HG)
TORR ABSOLUTE "L . #
POSTTEST B.P. 2.
-------
CLIENT
P '/9
PARTICIPATE WEIGHTS SUMMARY Page of .
Placed in Dess icator: Date/Time/o - S" **/
ES PROJECT #/? /2
RUN Ho.
STOVE MODEL N
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
)6- 5S
to - O
/'I'^.C'
9V7- S?
FRONT
PTF.TRR It
3/9^-V^
- yz.37
*/i^5"
. /-L35"
> /^/¥
a 00 Z/
BACK
PH.TKR It
S«?/-W
. y-2.z-o-
* /^. /"?
* /i /•?
. /z/t.
»O-C'C'5
CALIBRATION WT.
WT AMOUNT -
PRE WT
. ^£>£>O
C ^Cx? C>
POST WT
„ £oo6^
^/ ^^^-^-^
BAROMTRC
PRESSURE
2«?,7^
^-9,^0
Initials
t
/H«y
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of
CLIENT {
ES PROJECT
RUN \\a.S/J-OPI~5A Placed in Dessicator: Date/Time_Al
/loo
*-^& / ^
9j <~> O* M
OH. f ^ => Q /
BEAKER \\
/)-vs
69.73 *o,crrt/
POST WT
5<9. O&O/
V 9- 9 979
ROOM CONDITIONS
RELATIVE
HUMIDITY
a.c^
tic,*
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
- "7*1
'0
.00 9"7 (C)
TOTAL PARTICULATE CATCH (A+B+C
-------
CLIENT £l
ES PROJECT P*D\ 2.
PARTICULATE WEIGHTS SUMMARY Page _ of _
RUN No. S#-OP2-^& Placed in Dessicator: Date /T line /Q-S"
STOVE MODEL No. /9A> /
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/0- <•
/<)<•<:
/o- ^
/•^ 1&
9-/7^?
FRONT
FILTER It
S^-V/5
. /-z.^.^
- /Z7^
. / z^S"
• /Zo't
. oo/&
BACK
FT[,TF,R 11
5V9^-V^
.no/
• iTLco
» 11-00
./*oQf.
— , ooe>*%
CALIBRATION WT.
WT AMOUNT =
PRE WT
/ 5 6&t>
> ^ 0<°i{)
POST WT
> *)&0/)
"» *>£>&/
ROOM CONDITIONS
RELATIVE
HUMIDITY
V&6V
V^^7-?_
BAROMTRC
PRESSURE
-Z-9. 7^
7_ 9, C n
Initials
1
/>c>f
^ c^
I
Ul
I
(A)
(B)
-------
CLIENT
ES PROJECT P\D
PARTICULATE WEIGHTS SUMMARY Page of.
RUN No. S^'jJPf-SS Placed in Dessicator: Date/Time.
STOVE MODEL Nn./)/^/V
POSTEST
/O
Acetone Lot __
Acetone Sample Volume.
// b
"70
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
j.
TARE WT
NET
DATE /TIME
!<>-(,
11 tt,
lo-t,
•^0 / S
Q -/tf-89
BRAKER 11
^- 74-
6^.99Vo
f^.ltY/
^9,^?y/
£> . Cn:*) /
POST WT
£>O'Ooo/
V?.99?c/
ROOM CONDITIONS
RELATIVE
HUMIDITY
V<£<2^ «
V^^7?
BAROMTRC
PRESSURE
29- 7V
^'t-O
Initials
J»cf
MKZ/I
•n
i
CO
Cd
I
01
I
OO
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
• o o I
(C)
TOTAL PARTICULATE CATCH (A+B+C) =.
_rng.
-------
Page
of
CLIENT
PA
ES PROJECT A/) /2 3
PARTICULATE WEIGHTS SUMMARY
RUN No.S^'^-S/Q Placed in Dessicator: Date/Time_/£jJ/_
STOVE MODEL No.
POSTEST
Acetone Lot (\_ct//.&'_ __,
Acetone Sample Volume -^ /
WT 1
WT 2 .
WT 3
WT 4 '
WT 5
FINAL WT
TARE WT
NET '
DATE /TIME
10- (f
If Of)
10 -4
-T-0 /<,
9-/<3-?7
BEAKER II
/9-V?
07, 2953
£7- 2C/sy
^^.-z'y^y
<^7.7 ^?0
o , 06^; v
CALIBRATION WT
WT AMOUNT =
PRE WT
^0 , 00O S
^O, &VP /
POST WT
^~ ^^
^f-
-------
CLIENT
ES PROJECT P\P
PARTICIPATE WEIGHTS SUMMARY Page of.
I
RUN No.S/y-'Xj--'^/? Placed in Dessicator: Date/Time /6 ~ S' ^
STOVE MODEL No. /PA'"/
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
lt>- (f
}0 tyO
1* - (f>
<"? -7.O
9-/7-S?
FRONT
FILTER II
/)£- V 3
,11-00
,-l/?cl
-7/99
.6*237
. o 36, Z
BACK
KTr.TKR II
/^"-vy
. <^«yy
* 6 «£ V 0
,6^>/o
. 6^00
o ot> Yo
CALIBRATION WT.
WT AMOUNT =
PRE WT
v ^ 6&O
» ^O&&
POST WT
, $ o O 0
e ^£>T> /
ROOM CONDITIONS
RELATIVE
HUMIDITY
vts^
V-^^7 Z.
BAROMTRC
PRESSURE
Z'^-7^
' ^. 60
Initials
t
y*i^^>
^f $
i
i
i—•
o
(A)
(B)
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
-of.
CLIENT
PA
ES PROJECT f\D
RUH N0.5//-9S-5/? Placed in Dessicator: Date/Time
9TOVE MODEL No.
POSTEST
Acetone Lot It
Acetone Sample Volume
"67
WT 1
WT 2 .
WT 3
WT 4 '
WT 5 '
FINAL WT
|
TARE WT
NET
DATE /TIME
)o - if
l/oo
/^ - <-r
-2-d> / 5
9- 'S-s?
BEAKER It
/?-VEr
C7£Z-?9
67. ^zy^
<^7. 62V^
67, ^Zc>/
P CrOVL.
CALIBRATION WT
WT AMOUNT -
PRE WT
£<3. ot>o /
^ C> t C"f<& /
POST WT
$a • Q66/
V?'??'?'?
ROOM CONDITIONS
RELATIVE
HUMIDITY
<-/%£>&%
V-Q&-?-?-
BAROMTRC
PRESSURE
-2.3, -)1/
^- 6 o
Initials
rȣ#
fac/£
X.
I
Crt
w
I
Ln
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICIPATE CATCH (A + B+C) =.
jng.
-------
CLIENT C_
ES PROJECT A D
PARTICIPATE WEIGHTS SUMMARY Page of.
t
RUN No.S'V •*>&•• £73 Placed in Dessicator: Date/Time.
STOVE MODEL No. A/< - / ^
POSTEST
' WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE WT
WT GAINED
.DATE/TIME
If- <*
/a So
/&-
, 6^y6
*6s/3
- 6 3/3
-679f-
, CT^^9
CALIBRATION WT.
WT AMOUNT =
PRE WT
l *~>06C>
„ ^fX'O
POST WT
, Sooo
f 5"<5T? /
ROOM CONDITIONS
RELATIVE
HUMIDITY .
V«^j»%
V^Ck^?"^
BAROMTRC
PRESSURE
29- 7f
-Z-l.to
Initials
t
XH CX?
^>c^
EC
I
Ln
I
(A)
(B)
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client fa"PA- Run /
Date /b^*-/ ~ ' ~~
ES Project |
Wood Heater Model
Operators
1
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) ^O Secondary Air Setting
Achieved Burn Rate (Kg/hr) \\o~l~l Thermostat Setting
Primary Air Setting l*Agyc. 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
. 0
C.ecrO
Post Test
77
TEST FUEL DATA
Firebox Volume (ft)
Fuel Charge Range Wt. II* (^ to
Actual Fuel Charge WtAj,/
Coal Bed Range Wt.^T to 3
Actual Coal Bed Wt.
Fuel H20% Dry
Fuel: Dry Kg /R,
By-pass
Door __£
Yeloci ty Traverse
LOADING/TEST START OPERATIONS
^S-^J Air Settings
I i*-^.l->. Comments
p Temp
A 1
2
3
4
B 1
Ave . . p
Pitot Leak Check
Static
F-SH-5-13
-------
ENGINEERING-SCIENCE, INC.
Client £m -U-fcL Hun S
Date /0- 1 -
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ued
' Wood Heater Model
ES Prbjec. I /yp 1 7,3* Operators
3. "^
Page / of ~3
Time
Sanipl i ng/
Clock
o
v^-V. \ "?,.
Catalyst Temp
Prejlntemail Post
'37^
(lit-/
///tf
//s/
973_
c)Vu
-) z-
int
11 So
i/SS
/tfct
loll
Top| Rear| Uottom |Right; Left
55=7
VVJ
Surface Temp.
270
7? 3
.7 "8
5V/
_23j
2V.
•270
^L
/5
'35
hi -I
s/Z.
^I2L
60O
6/8
Z.o
Stack
Temp .
"DO-/
Oil .
Tun .
Temp
8S
II
9s
9'i
Room.
Temp .
20.
7T
75
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £-{V3-Run
st-s •
Date
Wood Heater Model
Test Fuel Charge
Coal Bed
Page
of
ES Projec, f Kb 1 2/3 Operators jti H ~ filc ft
JB
I
Ul
I
I—«
Ul
Time
Sampl ing/
Clock
l -3,
Test
Fuel
Wt.
(Ibs)
Oof
16, 1
_ki_
Flue
Draft
(In
H?0)
o ,
0.6 ?O
6.065
6,0
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £ /9/9 Run
Date
ES Projec
5 // - 5
Test Fuel Charge
Page "3> of
• Wood Heater Model /?AV/5 Coal Ded
Operators Hi f l\
i
to
PC
I
t_n
I
Time
Sampl i ng/
Clock
l-h
I "tS
-T-oln
7-°W?
Test
Fuel
Wt.
(Ibs)
1,0
on
±^L
7.* 5
0 *0
Flue
Draft
(In
H?0)
060
/0 7 A
ftiQlft.
ft, (>(••$
6 s
(j.e
ePtft
Comments
C lr>
dital.yst Temp
rt nternal Post
//5V
A'//
90 V
7-7
/Oil/
/V/
II
f"3
10-7-7
(o'Ll
tool
522.
•-7'V
l^/^
lop Rear Ltottom Right Left
6/0
5" 76
Surface Teinp
362.
3V o
536
33
V//
V67
S
VT/
5V/
6 1>' S
Stack
Temp .
V53
5 2V
J3i
V77
Oil.
Tun .
Temp
9S
lo'L.
/0~0
T7
Room.
Temp .
"76
75
76
77
77
77
77
7?
77
ZZ.
77
77
7?
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater f\^~' §
Date /o-v - ©^
Sampling Location ^T=«-2_
Sample Type
Run
Start Time AJ V U
Stop Time
Probe Length and
Type ./2/'
\rt^6i Pi tot Tube Coefficient , Q c/
Number 5 /•/ - £6 - ^/9
Operator v/OblH i -JMcK.
Ambient Temperature
Barometric Pr(
Static Pressur
js*sure
^e, (Ps)
Assumed Moisture
cj
Sample Box Number
Meter Box Number
Meter H
l^~-<~> - ~^
Pretest Leak Rate o,,/o &£ ~? "
Filter Number(s)
Meter /,
oo 7^-y
Post Test Leak Re
i
Read and Record All Data Every
Clock Time
Sampling (24-hr
time.min Clock)
C? IGC^CJ
t& / ^ S °
•2& I \C>O
,?£> \\\e>
*•/& in.o
to l/3o
~7o i \ $£>
30 /2.0O
90 /2/D
/CO /?.?,0
//^ J??>0
/ 20 / ? /1/u
tloC /32o
/?£> /^^
/ftO /3Vo
/9C1 /^5<^
7/X7 ;v^
Ito W/o
1fL,£> /V2°
? 1 ^ A/ '^
3-Yt> l*-Wo
Gas Meter
Readi ng
(VJ ft3
32> /. /
3^/.o
T?£/. o
35^. 1
7ic0j , j
36,6* 7__
"SI /• 3.
• "^,7 6> , 3
^.a/. 3
1>?s4.^-/
"^ /<^y
^"i ' V
4/0/,<-/
-yo^.iy
y/y* s
vy^" 5
V2 X« ^T
^/^^. 5"
A' 3 / • S
V 3 6 . V
//^^ ^
//V4- . y
Velocity
Head
( PS), in-
H?0
/j (^(— i 1
.f} O*^ /
6'0>V/
^>^Q L^ /
fr.O'-t I
cxo<-/7
&.&<-//
O.^i-t I
b-O1-/ (
0.0<-//
. . o °V
,& c//
/O1-//
eV-f/
, c^V/
, o<-//
,C.
, QO
- SO
«B
zro
.
. Xo
. ^3
, ^o
« S^O
, Xo
r /> O
, Kc
p «5^
_ <;) fj
0 ^C>
.X'O
. 5^0
, f?ci
, ?iO
i 3t;
Actual
>f-->o
'^1(0
r SO
. B'C:)
• "fiCJ
' f^
t&O
• So
- ^b
, tfo
- ^O
i Ji'o
, ^c.
. ^0
' VC>
, >;ci
* T j n
, Z^.)
.20
, Ko
s^'
, &j
. S-'o
\tQ£>fo/fc> (*& fr "
Minutes ^
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
<£eS"
"73
•78
$"£_
&1-!
as
s~i ~
©&
BS
^'?
^v'
^>
90 -
'/C)
^'<9
r/a
C'/
9 /
9
7"^ V ~7
7 ^ V ~7
7v "o
T7 57
77 V9
7 ^
2_
'2_
?
"2-
Flue Draft
in. HoO
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont,
Wood Heater
Date
O
(O
Sampling Location
Sample Type
Run Number
Operator
C,
A
-zy.3
Cl
Sampl i ng
time, miii
ock Time
24-hr
;iock)
Gas Mater
Readi ng
(vm) ft3
Veloci
Head
UPS)
ty
in.
Ori f ice Pressure
Di f ferenti al
(AH), -in. H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
U.
Filter
30-
Impinger
Dump
Vacuum
in. Hg
Flue Draft
in. H20
7
/
77
5/
A
-77
77
2.
.go
97
-2,0
, ?, 0
^LL
92.
7 8-
2-
&<-/1
9/
j£Z.
6=.
, 5
, Ko
78
n?o
/7?0
77
"7?
77
5' A
77
PC
I
Ul
I
±.
V/
8
y
7 V
1,
2-
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater /)/<-/
Date
Sampling Location
Sample Type "2.5-/
Run Number
Operator
'/- S •?
"\^ Clock Time
Sampl1ng\(24-hr
time, minX£lock)
~ff~^cT dJkj&!_
<-/ -/S*fc
V fa/o
<^~i. o /CfZo
5-^cJ / / 9 ~l.o2o
^ o lo 3d
(fat) ~2c/7
Gas Mater
Reading
(vm) ft3
^^.y
^•?/. v
^76. y
5"a/-4
5S£,, 6
5?/, 7
^•7^. 7
^ /„ ^
/^* 7
62./. ^
6->~L~7 * r>
<&^^- • (O
/y.3<^, ^/>5~
~b)o.5crt>
Velocity
Head
UPS) in.
H90
.*V/
* a <-//
»(>H i
o o HI
>"<-tt
0 *V/
, oV/
*-
' . So
a S^J
« Sc^
»So
- ,Vo
« So
<. 5^
<• s"<9
u So
• .^
Actual
/ S^
« s^-.
, '/<^
( ?>0
<• f)0
, r; ^
' So
-
-
9 7
^^
97
97
97
9>-?. -
9 -7
77 -
'
9o:3
Filter
-? ?
•?So
8/
S/
ft/
%' /
^/
s /
^o
«o
<^o
??
7"?
"7?
7 25
Impinger
C7_.
^/
S".
'Z-
-z.
-7.
"2-
7.
Flue Draft
in. H?0
EC
I
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number
Operator
Ambient Temperature_
Barometric Pressure
Static Pressure, (Ps
Filter Number(s)
Meter Y— > <_>
Start Time
Stop Time
- ^v?
IX
I Kr ^
Probe Length and Type_
Pitot Tube Coefficient
Assumed Moisture ~
Sample Box Number
Meter Box Number <
Meter H
Read and Record All Data Every
Pretest Leak Rate
Post Test Leak
Minutes
/
Clock Time
Sampling (24-hr
time.min Clock)
Veloci ty
Head
( PS).in-
H20
Gas Meter
Reading
ft3
Ori f ice Pressure
Dj f ferential
( H), in. HpO
Desi red
Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H0
6
,9s
/o
-7S
TO
U^»°
"b
7°
"77
77
77
?', 7
Q.
:^"7
-77
77
5-90.8
,9-S
, 95
77
-------
ypazu f aa^a
|t-.-rrra tissjx
S,T7?va ^^'~^
Operator / \ /./ M i < \J^{\
i
CO
PC
1
Ul
""\ Clock Time
SamplingX^ZA-hr
time, min\£lock)
•
"Z-SO /V5O
~2&>c> i^o<^
770 /3YO
"7 ?<£> /5^O
"29° /S?'2'
"3^o / 5"Y#
3/C> I'S'-tO
o2c> /£>£>£>
330 ,^,o
3^"° /62-0
39O /6>^
U&O /t-^VO
•^7C
o£c
i> /61?0
> /9^
"370 /7/<3
£/£X-^
^//&
/720
t-fio n^t*
L/30
/ 7 '?'£>
> /£^°
^5-3 f&i'O
tbt
L17
' I&2&
s (£i"7O
Gas Meter
Reading.
(vm) ft3
x ^- q-, S'
^,^ a , 7
(tdtS e 7
<£>7<9, 7
<^ So« 7
^j^^ 7
<^9o . 7
/?•??"» 7
7^20. -7
7/0. 1
7ZO, 7
1ZS". 7
7 3° '-7
735 -7-
l^o, ~~j
7^c?i 7
'") 50 . -7
•-) 6,0 , ^
Velocity
Head
UPS) in.
H?0
O-O1-//
,C>*-Y /
'O^y /
o°//
, ^^/^
to^f
Q1-//
dL/ r
,OL//
v/
»OH/
eOH 1
* OLil
Orifice Pressure
Differential
(AH), -in.
Desi red
, Vs
,9^
.9s
,9-e;
', 9S
.SS"
.•55
, S'<^
• vc
.95
' V S
. c/5'
. 9-5
i ^S
.'7*^
c fe
,9^
,->•<,
, 9 'S
,, <7<7
< f( ^
H20
Actual
/9S
,9^
i9s
<^9S
r9S
,95
.9s
'9s
, S5
* 9 T
.95
.^"S
' ^S
, ^Cj
'3 ^"\
^^
<-9S
t 9S
' 9 9
' 9" 9"
- 9 9
TEMPERATURES
Di lution
Tunnel
Meter
In
-
Meter
Out
9"6»
Cf ^
cl ^
*•) *>
9 Cf
9s 6 -
9
9 <^
9 <>•
?&
CfLe -
9 L>
96
(f
1£
*i<-<>
9o -
V6
/?(Y
9 £
9 /,
9?
Filter
Ao
7C/
~7 4
7 9
7<5 •
79
1f o
<* °
<^/
c?/
2*7
S7
S/
Go
Qo
c?<3
%*O
<^O
•70
7 Y
s ^
Impinger
^-i,
66
^ */
S- 4/
$'X
$•£•
•T <^
^"7
5" 7
5 "5?
5"?
(p0
/„<>
C 7
X* *>
^ i.
^3
fp-^
£, 3
/
(x O7
Pump
Vacuum
in. Hg
^
^5
.7
3
j?
-^
3
3
•?
•^
3
3
7^
^
~\
-\
3
~\
3
S
3
3
Flue Draft
in. H?0
-------
i ^mljt
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater /)K - /
Date /x> -
Sampling Location
Sample Type 7. g
Run Number
Operator /
~ If 7
\. Clock Time
Sampling\(24-hr
time, min\£lock)
~H~77>~~ — - — — ^5-Ii
V£o • /V$Vo
V 9 o / t> To
Tf j 6> / 7 t?f>
^/d 1^/0
52.0 A/20
^~3o /?~3^
^-Ko /"79b
^5~0 /?^£>
5 4>o "Z^ £>o
•?"7o -^.£vo
9^5^ -Z^zo
57^ tZolfl
fr&CJ ZCVfi
^ « ^~
•s// . ?_
S/6. "^
"
99 -
c^
Filter
J5/
ft7_
^T,
S^,
«.1
5? ^
^ T
C3
ff "?
^ 7
fr-z
« Z-
f? ?
«7.
75 ,/
Impinger
6 -2.
SV
^ f>
5^0
5"Q
To
.Sr>
S -2-
s?
5-/
S2
5-7
^7-
.5"Z
9^
•
Pump
Vacuum
in. Hg
-?
'3
•3,
^
3
1
^
"3
1
-?
..•?
^
•?
^
3
Flue Draft
in. H?0
I
CO
PC
I
-------
FUEL MEASUREMENTS
Date I&-H - S^ Wood Heater Manufacturer
Project No. £b >Z-^> Wood" Heater Model_
Run No.
Circle One: (Tretest^Eael Test Fuel
Fuel Type and Amount 2x4 Ls 4x4 1x4
Ideal Load Weight ; Actual Load Weight ~
Fuel Piece Length . /\^ (a 'f .
Moisture Meter Calibration 12% \ -i__ 225 "2_-x-
Moisture Content- (Meter - Dry Basis)- Co»v*c7t
-------
FUEL MEASUREMENTS
Date
Wood Heater Manufacturer
Project No. £ fc> /2--\
Run No. *:^U , <^
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
WoocT Heater Model A^- f ^
TeVwiel
2— 4x4 "*<_ 1x4
Actual Load Weight
Fuel Piece Length / ~7
Moisture Meter Calibration 12%
/ ~L- 22X -2_~v_
u-vp
Piece No.
1
2
3
4
iU
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)—'
Readings Average
Z/.3 2/-/
/41
Zi.l
E2.C,
3.8 Zf/,6,
^.o 23.7
Overall Fuel Moisture Average
F-SH-5-24
-------
TEST
SH-6
D12340
J81AAPP
-------
Method 56 Proportionality Rate, Flow Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: Sl€ET HOME
Model no: RK-18
Lab name: ES
1st date: 10-5-89
Run no : SH-5G-6R
1st time
(min): 578.00
Chrg ut
(Ib ueth 34.80
run
time
(min)
0
60
120
180
240
300
360
420
480
540
578
vel dp
(mm
(in
0
0
0
0
0
0
0
0
0
0
0
H20)
.H20)
.039
.039
.039
.039
.039
.039
.039
.039
.039
.039
.039
Units l=metric,
2=Engl ish:
Y, DGM:
Pi tot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (7. uet):
Burn
stack
temp
(C,F)
85
90
92
88
93
91
91
89
90
90
90
DGM
rdg
(m3,ft3)
636.602
666.400
696.500
726.700
756.900
787.000
817.300
848. 100
878. 100
908. 100
927.623
DGM
temp
(C..F)
66
90
95
91
92
92
93
92
91
90
90
Samp vol
2 (sm3,scf)
1.007 281.303
0.99
28.56 Flou rate
29.82 (dsm3m,dscfm)
0.1963 145.26
18.87
rate (dry kg/hr): 1.33
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
vel
(m/min)
(ft/min)
802.23
805.90
807.37
804.44
808. 10
806.63
806.63
805. 17
805.90
805.90
805.90
PR
(2)
103.4
99.8
98.4
100.4
99.0
99.9
101.0
98.9
99.0
101.9
85.49
17.640
460.00
1850.00
dDGH
vol
(m3,
30.
29.
28.
29.
28.
29.
29.
28.
28.
18.
std
ft3)
067
047
881
090
941
134
561
845
898
840
vs/VmTs
0.01
vs ave stack
ave temp
805.83
(C,F)
89.91
i
CO
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(rain):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
•120
480
540
578
SWEET HOME Units l=metric,
RK-18 2=English:
ES Y, DGM:
10-5-89 Pitot co:
SH-56-6B Gas MW :
Pb (mm, in. Hg):
578.00 Stack area (m2,ft2):
Hood moist (.2 uet):
34.80 Burn
vel dp
(mm H20)
(in.H20)
0.039
0.039
0.039
0.039
0.039
0.039
0.039
0.039
0.039
0.039
0.039
stack
temp
(C,F)
85
90
92
88
93
91
91
89
90
90
90
06M
rdg
(m3,
836.
866.
896.
926.
956.
987.
1017.
1046.
1076.
1106.
1126.
ft3)
604
400
500
TOO
900
000
000
900
800
700
118
DGM
temp
(C,F)
65
89
97
96
95
96
96
97
97
97
96
Samp vol
2 (sm3,scf)
1.024 282.975
0.99
28.56 Flou rate
29.82 (dsm3m,dscfm)
0.1963 145.26
18.87
rate (dry kg/hr): 1.33
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
vel
(m/min)
(ft/min)
802.23
805.90
807.37
804.44
808.10
806.63
806.63
805. 17
805.90
805.90
805.90
PR
(*)
104.8
101.1
99.1
100.5
99.6
99.2
98.5
98.7
98.6
101.1
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
30.
29.
29.
29.
29.
29.
29.
28.
28.
18.
std
ft3)
631
591
263
315
271
121
024
972
972
815
vs/VmTs
0.01
vs ave stack
aye temp
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED /Q -*£- % 9
DATE RETRIEVED
WEIGHT GAINS
PROBE '
LINE
CONDENSATE
FILTER*1
FILTER//2
TOTAL (MG)
TEST LOCATION'S- ti) S - < /? ft
SAMPLER SN//_£2_4_2J>JL
(HG BAROMETER UNCORRECTED)
PRETEST B.P 27.'?''/ (IN HG)
TANK Z5-S5 ("IN HG) TEMP. Z.O (C)
TORR ABSOLUTE "2-» ^
POSTTEST B.P.-2L9, 7 fr (IN HG)
£>.l, RUN,?
O .
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED / 6 - $"- S
DATE RETRIEVED
TEST LOCATION £ 5 - l<) S ~
SAMPLER SN// 9 6 "2 1 V
WEIGHT GAINS
PROBE
LINE
CONDENSATE
FILTER*1
FILTERS
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(HG BAROMETER UNCORRECTED)
PRETEST B.P_ZV^_(IN HG)
TANK 2/7, 65 ( — IN HG) TEMP.
TORR ABSOLUTE ~Z- • 3
TOTAL (MG)
(C)
POSTTEST B.P. "2.9- 7^ (IN HG)
7-So
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PRETEST LEAK CHECK
RUN* $/-/- Q
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STOVE ID /? /C" - /*%•
WOOD SPECIES
f, IA
WOOD MOISTURE (% DRY) "Z.'b, lp
WOOD MOISTURE (7. WET) I 8 . g ~7
WOOD CONSUMED (LB) JH8_(KG)|5jj
SAMPLE FLOW RATE PRETEST
POSTTEST
ROTAMETER
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START
(IN H30) FINAL
(IN H20) LEAK RATE Q , Z, (IN H20 MIN)
POSTTEST LEAK CHECK
START H.t (IN H20) FINAL . t y
c •£/
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GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE+FITTING
SAMPLE LINE
CONNECTOR
MIN. +JJ) MIN. +\l. MIN. + MIN
32,3857
PELTS
F-SH-6-4
-------
CLIENT
P ft
(PARTICULATE WEIGHTS SUMMARY Page _ of -
RUN too.Sk-l)Pl-6>A Placed in Dessicator: nat.«/Tiina ff> ~ (o ^
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STOVE MODEL N
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DATE /TIME
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-------
CLIENT ±
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PARTICULATE WEIGHTS SUMMARY Page of
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STOVE MODEL No. /) k- /ft"
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Acetone Sample Volume
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-------
CLIENT
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PARTICULATE WEIGHTS SUMMARY Page of.
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STOVE MODEL No.
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WT 2
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WT 4
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TARE WT
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DATE /TIME
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°
Initials
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(B)
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CLIENT £"P/)
PARTICULATE WEIGHTS SUMMARY Page.
RUN No. ^H-l)PI-6ft Placed in Dessicator: 1
.of.
ES PROJECT &f) /2 3 8TOVE MODEL No. A )< *
POSTEST
Acetone Lot It.
Acetone Sample Volume.
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NET
DATE /TIME
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CLIENT £ PA
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PARTICULATE WEIGHTS SUMMARY Page of.
RUN No. £W- <£<£•- (off Placed in Dessicator: Date/Time.
J2.3
STOVE MODEL No.
POSTEST
Acetone Lot it .*)// *X
Acetone Sample Volume.
WT 1
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WT 3
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-------
CLIENT £
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PARTICULATE WEIGHTS SUMMARY Page of-
RUN No.t>./y~56 '4>9 Placed in Dessicator: Date/Time/O-6^ /^V^
STOVE MODEL No
POSTEST
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WT 2
WT 3
WT .4
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DATE /TIME
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PARTICULATE WEIGHTS SUMMARY Page, of.
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V ?.o ,000 /
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-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
0
RUN No.g/V ' £<£ '«£/? Placed in Dessicator: Date/Time.^
ES PROJECT KD /"2-1
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WT 2
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Initials
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-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client ' ''Eft/I Run / '^'(4 "6
Date /O /S "S °T ~^
ES Project
Wood Heater Model
Operators U
4 /£
TEST RUN INFORMATION
Attempted Burn Rate (Xg/frrf S3-J Secondary Air Setting
Achieved Burn Rate (Kg/hr)
Primary Air Setting
3
-
Thennostat Setting
Other Settings f\J /\
f\]/V
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
7.9, ??
-7-L.
Post Test
-73
TEST FUEL DATA
Firebox Volume (ft-)
2.0
Fuel Charge Range Wt JZ.. ^ to /6.L
4/ . .. ° -L #3
Actual Fuel Charge Wt.!
Coal Bed Range Wt. ~2-<* to
Actual Coal Bed Wt. "S
Fuel H20% Dry 11.1
Fuel: Dry Kg \1
Wet
LOADING/TEST START OPERATIONS
By-pass C'lo^-^r Air Settings
Door QI^J?,^ -^ ISsg'C- Comments
o ^
Veloci ty Traverse
p Temp
A 1 6-030 A^ B 1
SQ
P
3 (D.QUJ5
Pi tot Leak Check
Static
F-SH-6-13
-------
Tl
I
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WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £-VlRun
SH -
Date
^"5
ES Projec. |
Time
Sampl i ng/
Clock
o
H^o
I60O
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Test
Fuel
Wt.
7,
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Page
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73
-------
ENGINEERING-SCIENCE, INC.
Client GPA Run I
Date /0-S~S°(
ES Project I
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators UHJrf ,
Page
I
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Time
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72.
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7V
7S
75-
75
75
79
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERINGS-SCIENCE, INC.
Client £- P/l Run I
Test Fuel Charge
Page 3 of
1
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ENGINEERING-SCIENCE, INC.
SAMPLING OATA
Wood Heater f\l£r/_O
Date '£>'-^> - B^/
Sampling Location hT^~?_
Sample Type
Run
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Probe Length and
Type . )~i~"
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ENGINEERING-SCIENCE, INC.
MPLiiNb UAIA ^onc. ; / »
Wood Heater (\ K - / &
Date
Sampl i
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Type
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75
7S"
7*5
7^
75
"75~
7 5"
/'y
9y
7 '
~5_
~2-
2_
"2_
2.
^
~^
^
«-_
Flue Draft
in. H?0
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood lleater_
Date
/-I
/o ^
Sampling Location
Sample Type
Run Number_
Operator
3/3
\. Clock Time
SamplingX^A-hr
time, min^v£lock)
~ — - —
Yfto nso
£V? o ^fioo
£cro f&/o
5/0 (<&'2c>
^-2-0 /83£>
S3o f<9?S» /
^;?. o
^ar.o
Vo^.,0
^09^ /-
*?/•?* z.
7/9T. 3
~2>cf
6f o~Vl
3. & 3 r6^
- 80
. S'o
,
^o>
- er^j
• So
• ^?c>
o SO
. f>0
Actual
/ 5"0
,-ito
/•So
.s-o
• s^o
• 80
^ Go
-80
<• ?So
,? So
^•^0
,9d
TEMPERATURES
Di lution
Tunnel
/.
V
<\t>.\
Meter
In
(
-
Meter
Out
9/ -
11
i
7y
Vcy
•7^
93
71
7Z_
•7Z,
7.3
Impinger
S^
^•r
^7
•5"?
^~i
•S-7
5-^
5-7
5"7
s^r
^^
-
Pump
Vacuum
in. Hg
"2_
'2_
^
2_
^__
^_
e.
•^_
2.
"2.
^
Flue Draft
in. H20
EC
I
I
i—'
VD
-------
i^^ft
ENGINEERING-SCIENCE, INC. SAMPLING DATA ~J)
Wood Heater A^"' & start Time
Date /a ^ -fi>c/
Sampling Location "KT^-x-
Sample Type |
Run
M JT v-
Number ?SH - ^ 6 -oo>
"2.0 fO(&
3O IO2&
yo /£> 30
90 /av^
£6 /C-£<3
70 /fc>o
9D //^'
*££> /^2O
/OO ^5<>
y/t> ll'-fo
l?o Il5<3
f TO / 2^
yvo /^'o
/"Tb I73-0
/fcO /?-?6>
/7& /2'VO
//?0 /" 2^
f9 / '-iY50
?OO /'5/c>
2/o /320
7_?£> C "VZ^
•7 ^,£> / ^%^-o
•2. 'ycj / 3^0
Gas Meter
Readi ng
(vm) ft3
fi^.^O*-/"
(T^/.S
W^"^
K^'A V
^Co . ^-/
^/< ^
^6- .V -
f>j /t, ^
Oi ~7/ / ./
CJ / w - ^/
•p: / <_/
A;
• 3 "
c?9 /, , S
_9/ L C»
"7/6, ^
'?? / , 7
VZci. -^ -
C?-^ J O
*-'?^^ - c >
GJLJ i O^
u/ y CP , ^
c?^ i ' ^
Velocity
Head
H2o'
• 63C/
0^^
.039
• °?>^
, ^Ti^
,039
,6-3/7
,o>"2,9
, c>39
. i c>-2, cr
i^"3^
/ o "J c}
, V
Orifice
Di fferc
( H), in
DesT red
, V'3
, 7S
."75
,9S
,95
, *?s
t °) ^
t > rS
< <7./5"
, 7s
* vs
.'y'5
. ^3
, "7-3
cV r?
. *>*:>
.9^.
• V*.
« V5
-^'b
, '/i>
^ *7 t>~
• ^ "b
. ? s>
. 9 "^
'ressure
jntial
H20
Actual
< 9^
, 9^
, 9*5
^f S
i VS
,4 S
*? b
- ? ^
' ^S
. ^5"
. ?-')
/ ^5"
, ?' "3
."/S"
, (7K)
i V'S
^.s
. f^
- VS
• S-^3
- '•* "S
^S
. -' -5
. *? "S
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
(^ -
(&&>
7 •:%
79
^7
& / ~
9z~
7Y
95
94
9^
•7S-
?7
^O
V-^
c?0- —
C/X
7^
c'"5
f}"71
'^'h
'r -~, —
Filter
7 / *
7^
7?
77
5o
5-7
S/
7Cr *?/
7v 5" 2_
76
7>j
-5
7^
3
~\
^
•^
3
J3
.3
•^,
•3,
-5
~\
^
-v.
-X,
"*,
~3>
Flue Draft
in. H20
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater /\K.-f o
Date
/o ^ S - ^ «>/
Sampling Location K7~ '& ~i —
Sample Type
i
CO
pa
i
\. Clock Time
Sampling\(24-hr
time, min^xClock)
• —
*25c> /tj&O
2-Cf O I *r{ ( O
1-io /YZ.0
2,%><3 /YJo
2.9
3^0 >5%o
"3y& i^yo
•Jcio I'S^C
'Z'lo / 6>&o
'7QO 16/&
•y-)o /(o2^&
tfoo r&'zo
Si/£> tb^O
*'l/~i£> 1 (jrfO
t/3C> • I7&&
t--f(-fC? / ~?t ^
^i^f) 1 7
fy&o ( 730
^770 / 7<-/^->
Gas Meter
Reading
(VJ ft3
94M
972.0
?~n. o
?9Z^cJ
?S 7. j?/ 7
( 0 "?£, 9
( O'-//, ^
i •'' Hk . r/ -
i £>5/, 9
I ^ 7?^? * /
• i A/ / C^
/ 06(p ,"§
/ 67/. S
Velocity
Head
(APS) in.
•'V {s
. ^37
.03 ^
• °3^
i O^*"/
o"3 O
,e>'J9
.03°?
•03*7
« 039
*o~$ 1
t & 3 *7
<» (? 3-7
^/
^>o 3 9
, <>3 ^
,0-3 ^
(6;-?c>
. 019
,03^
,67)^
•
-^S
•^5'
c Cf5
^T^
,9S
. *}*::>
.^•p
^5
,tf
.75
Actual
, C/O
,95
- ^
- ^5
. ^-3
.9f>
. ^s
5^s
. ^"S
,7^"
^ 9^
* ct r
j <9 5-
* 9 5"
•°9 5
<• 95
, "75
t"7S
,<75
< 15
•95
.*? -s
. v>^
fA1^^
mber ^ (4 ~ *^ Cr- ~ &7\
OP (^(r/l-Jr
TEMPERATURES
Di lution
Tunnel
Meter
In
-
Meter
Out
c?5
9^
^S"
1 (f
^6
?6? -
94
9'tt
ftf
^
9 6 -
97
^-V *" "X
9-7
?7 -
^7
97
^7
?7
97
Filter
'•?<§
78
7,5
77
77
77
77
77
77
77
77
•77
77
77
77
77
7<£-
7<^
77
77
77
77
77
Impinger
5^/
5V
5" 5"
S'S
5'^
5"S'
f^> ^_«
•£T~^
3"co
5"7
•S" R^
^ ^>
•<5" §^
<9
-5" 9
<^> <^>
£0
CfO
Q/
c* t
6 2_
ci> ^>
7^
~\
^
•^
^
-3
-^
^
.-,
"S
-V,
3
->,
3
3
Flue Draft
in. H?0
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
_____
Sampling Location
Sample Type V-l
Run Number
Operator ^
/o
G- -
^\ Clock'Time
Sampl i ng\( 24-hr
time, min\s£lock)
" " — — — _.
•#3o 1 7^0
t/9o t QW
600 /B/°
^/o 1820
5"Zo /7(*. & -
(o 8 J eft
loS^.^
i o"? /, 7
/ T9
^> , o ^^
o-^ ?9
^5,0 3 9
Ori f ice Pressure
Di fferenti al
(AH), -in. H?0
Desi red
.^S'
.I*?
,?<;
.9S
-9'3
.^>S
/^rS
,95-
.9^
«9^
»<-/s
Actual
,9s
,f}^
,9?
<7S
«
Impinger
^
^.
•?
,7
.3
-?
3
Flue Draft
in. H?0
-------
FUEL MEASUREMENTS
Date l&'% "8at Wood Heater Manufacturer
Project No. R 0 / 1 ^> Wood" Heater Model
Run No. CAV - C?
Circle One: l(retestj*el ^ Test Fuel
Fuel Type and Amount 2x4 ^ 4x4 Ix4
Ideal Load Weight .Actual Load Weight
Fuel Piece Length' ^(_er'
Moisture Meter Calibration 121/7
Moisture Content-(Meter - Dry Basis)-c°'*/l£c''"t
-------
FUEL MEASUREMENTS
\
r-l
fix)
Date /Q'S'&°r
Project No. g b / Z j
Run NOo ,Sl4 - O
Wood Heater Manufacturer
Woo
-------
TEST
SH-7
S\RD123.40
IM1381AAPP
-------
Method 56 Proportionality Rate, Flow Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg wt
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
180
540
588
SWEET HOME
flK-18
ES
10-6-89
SH-5G-7R
588.00
30.40
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
035
035
035
035
035
035
035
035
035
035
035
Units l^metric,
2=English:
Y, DGM:
Pitot co:
Gas NU :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Mood moist (.'/. uet):
Burn
stack
temp
(C,F)
86
87
91
91
93
97
97
98
89
91
89
DGM
rdg
(m3,ft3)
930.003
960.000
990. 100
1020.300
1050.000
1080.000
1110.000
1140.100
1170.400
1200.200
1224.215
DGM
temp
CC,F)
70
92
97
98
101
102
103
104
102
98
95
Samp vol
2 (sm3,scf)
1.007 279.094
0.99
28.56 Flow rate
29.66 (dsm3m,dscfm)
0.1963 137.01
18.88
rate (dry kg/hr): 1.14
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
vel
(m/min)
(ft/»in)
762.72
763.42
766.21
766.21
767.60
770.3?
770.37
771.06
764.82
766.21
764.82
PR
(2)
104.6
101.4
100.4
99.0
100.0
99.4
99.8
98.5
98.4
99.3
8S.-49
17.640
460.00
1850.00
dDGM
vol
(m3,
29.
28.
28.
28.
28.
28.
28.
28.
27.
22.
std
ft3)
879
786
623
098
230
180
224
361
992
720
vs/VmTs
.00
1
vs ave stack
ave temp
766.71
(C,F)
91.73
Ed
I
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
Tst date:
Run no :
Tst time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
540
588
SHEET HOME Units l=netric,
flK-18 2=English:
ES Y, DGM:
10-6-89 Pitot co:
SH-5G-7B Gas MW :
Pb (ram, in. Hg):
588.00 Stack area (m2,ft2):
Wood moist (?. uet):
30.40 Burn
vel dp
(mm H20)
(in.H20)
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
stack
temp
(C.F)
86
87
91
91
93
97
97
98
89
91
89
DGM
rdg
(m3,,ft3)
130.002
160.000
190. 100
220.300
250.000
280.000
310.000
340.000
369.900
399.800
423.811
DGM
temp
(C,F)
70
91
98
99"
101
103
103
104
104
101
100
Samp vol
2 (sm3,scf)
1.024 283.202
0.99
28.56 Flou rate
29.66 (dsmSm.dscfm)
0.1963 137.01
18.88
rate (dry kg/hr): 1.14
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
762.72
763.42
766.21
766.21
767.60
770.37
770.37
771.06
764.82
766.21
764.82
PR
W)
104.8
101.8
100.5
99.0
100.2
99.5
99.7
97.5
98.6
99.0
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
30.
29.
29.
28.
28.
28.
28.
28.
28.
22.
std
ft3)
395
336
065
532
718
616
616
470
470
985
vs/VmTs
.00
•
vs ave stack
ave temp
(C.F)
766.71 91.73
Cti
I
•-.j
i
t-o
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
/v-7
$#/)
DATE DEPLOYED
le>-6-%<1
DATE RETRIEVED
TEST LOCATION
SAMPLER SN//3.
(HG BAROMETER
PRETEST B.PZ*
TANK T.9,7<5
TORR ABSOLUTE
POSTTEST B.P.
TANK . /<5'3<
TORR ABSOLUTE
£-5-^5- 1.*>
WOOD CONSUMED (LB) ^5 3^'-^ (KG) 13-72
SAMPLE FLOW RATE
ROTflJlETER^; £"
POSTTEST
ROTAMETER t~) (IN HSO) FINAL^C,
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED ) O - 6> ~ %<^ PROBE /, t,
LINE -O.7
DAlh RhTKlhVEJJ
RUN# S/V- ^,^:r-7/?
• lHol I-LrlL -<>" (C)
TORR ABSOLUTE -2. . 5
POSTTEST B.P-Z9.7
-------
Page.
_of.
CLIENT .
ES PROJECT
PARTICULATE WEIGHTS SUMMARY
RUN No. CyV~iy?r->?PIaced in Dessicator: Date/Time
STOVE MODEL No.
POSTEST
__
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
to - v
/33^
/* - 1
//*> -5
<7-/7^<$
• /Z3o
./Z3o
• /Z/^
O.oofCn
BACK
FTf.TKR il
5/?/T-^2.
- yz /•?
• 11-11
. )-L//
./-L/G
~OPeX)e>/
„ $000
ROOM CONDITIONS
RELATIVE
HUMIDITY
y^-^sr
Vs^67
t
BAROMTRC
PRESSURE
^9-^^
•2.9.9 S
Initials
I
sfrcf
/XC/?
I
CO
PS
I
-j
I
Ln
(A)
(B)
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page _ _o£
RUN No. S/J-t/Pf-y) Placed in Dessicator: Date /Time
ES PROJECT RD /2 3
STOVE MODEL No.
POSTEST
Acetone Lot it
9//*6
Acetone Sample Volume S
>3 / 5
,.•,'
WT 1
WT 2
WT 3
^ WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE/TIME
/&- If
WlS
/ 6 -°)
Ifff;
V/S-89
WEAKER It
x?-SS
7 7, 7/fc 7 tf
-77.74»7<^
77.7^ 7<^
"77,760 ^
« 00^^"
CALIBRATION WT
WT AMOUNT =
PRE WT
^6 .&0&O
5o.0t>i>l
POST WT
^O* t>0#/
^f>, ofj(j~L.
ROOM CONDITIONS
RELATIVE
HUMIDITY
V5^%^ "
y
-------
CLIENT
ES PROJECT .(( 0 /"Z.3
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. l/o
D.oo/3
BACK
FTFiTRR II
5/>^-- 5V
. y2oc
• /)* 9
» IW<=\
• /Z6q
~~~ »o olo
CALIBRATION WT.
WT AMOUNT -
PRE WT
< £ ooo
' *l&0/
POST WT
a ^OO/
• 5 OOO
ROOM CONDITIONS
RELATIVE
HUMIDITY
vs<^*
Y^£7
BAROMTRC
PRESSURE
^9,**•
-------
Page.
of.
CLIENT _L
ES PROJECT Rf)
3
PARTIGULATE WEIGHTS SUMMARY
RUN Nn.S//-///?/'-7<3 Placed in Dessicator: Date/Time.
STOVE MODEL No. /) X - '7(
POSTEST
Acetone Lot it 3 //
Acetone Sample Volume
-7-gr
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
lo- ^
/o SS
9-/8-»9
BEAKER n
>9-S-£
9^29CS
/ ^S s C i Q>!
"~? ^*r "z Q /" o
7^.2B73
0 . ^>^<^
CALIBRATION WT
WT AMOUNT -
PRE WT
^<9 , OOOO
S*.***!
POST WT
5^d ,<5£^O j
50 • c>oo~~i —
ROOM CONDITIONS
RELATIVE
HUMIDITY
H$®4<&'
y^©^7
BAROMTRC
PRESSURE
2*7 ,4>Y
29-9^
Initials
/**•£
*e4
I
en
^j
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(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
"00 I 3
TOTAL PARTICIPATE CATCH (A+E+C) =.
rng.
-------
CLIENT £ P/9
PARTICULATE WEIGHTS SUMMARY ' Page of
RUN Nn.^/y-^Cr-"?^ Placed in Dessicator: Date/Time/ -Sf
/Q^o
\o- *
/o/<
^-/3-«9
BEAKER «
/)-53 ^
7?.3/ 75
"?S,.^/ 7ft
^ 9 • 3 / 7<9
78,3/33
, ooy^
CALIBRATION WT
WT AMOUNT =
PRE WT
•*)£>, 0COQ
Se^ ,exjc> /
POST WT
$6, 060 /
^o . ooo ~L
ROOM CONDITIONS
RELATIVE
HUMIDITY
vs <^£ ?-.
9S®6~?
BAROMTRC
PRESSURE
•Z9-<£^
^ 9'*) %*
Initials
sxe/?
/ri*4
EC
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A+B+C) =.
_mg.
-------
CLIENT
ES PROJECT HP /23
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. ^//- *>6:~)A Placed in Dessicator: Date/Time_/^L
STOVE MODEL No. A H - /9>
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
lo - V
x^S
/*- 7
// /o
^77-$^
FRONT
FTLTRR it
fie- Sf
• 7o S/7
. • 7*3 £b
.7o Vo
'dl^l
O.filV*)
BACK
FILTER It
/fcf-5-2.
.69 ;^
c6<$lf
,66//
, 6773
0o^y/
CALIBRATION WT.
WT AMOUNT =
PRE WT
, ^"<30
.Zoo/
POST WT
« £"€'/
« 5*^^^
ROOM CONDITIONS
RELATIVE
HUMIDITY
v-s^ksr
y^-^i?
BAROMTRC
PRESSURE
•29-^^
•2.9-^8'
Initials
s
^f^X7
^ic^
I
CO
(A)
(B)
-------
CLIENT
P/9
PARTICULATE WEIGHTS SUMMARY ' Page , of.
RUN No. SyV-^r -78 Placed in Dessicator: Date/Time.
ES PROJECT fiD /23
STOVE MODEL No.
POGTEST
Acetone Lot U
Acetone Sample Volume *?TC?
WT 1
WT 2 .
WT 3
WT 4 -
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
10 - ^
/ - 1
/^) ; ^
9-x^^f-
BEAKER it
/)- ,ae&l
POST WT
$6 .OCia /
<^e>. 6001-
ROOM CONDITIONS
RELATIVE
HUMIDITY
vsQ&sr
V^S!&7
•
BAROMTRC
PRESSURE
Z9-^^
i9,9^
Initials
y«f c>f
/***•*
I
CO
PC
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
* 0797
(C)
TOTAL PARTICULATE CATCH (A+B+C)
rng.
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No. 5A -56~~JA Placed in Dessicator: Date/Time_^>_2-.
ES PROJECT KO /23
STOVE MODEL Nn.
POSTEST
WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
lQ -V
/^^5
lo- °\
1) 10
9-/7-S 9
FRONT
RTLTRR It
/)£• 53
. ?o SXtt
*~)oS%
.7o?%
• 6>7&/
o . cOs\ 7
BACK
FILTER tl
/9£~ - $y
^V5
CALIBRATION WT.
WT AMOUNT =
PRE WT
t <£ <&&£>
• ^ o-o /
* ^3000
ROOM CONDITIONS
RELATIVE
HUMIDITY
ys®&'x
vj3>$7
'
BAROMTRC
PRESSURE
2.9. 6Y
T9.9K
Initials
6
><*fOf
^1^
i
i
i—'
NJ
(A)
(B)
-------
Client _
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run i
ES Project i (?
"Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) \^) _ Secondary Air Setting
Achieved Burn Rate (Kg/hr) /„ /<-// Thermostat Setting [\1 IV
Primary Air Setting Ipf*viu/v Other Setting?
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
73,7
o
/ o . O/ID- o
O.CfX)
Post Test
/ T
TEST FUEL DATA
Firebox Volume (ft-)
Z.C
Fuel Charge Range Wt. /Z.C to f5,t/
Actual Fuel Charge Wt. 'j^ 3oj"-f
I j, <'
V, 3
Coal Bed Range Wt. 2,7 to 3. 7-
Actual Coal Bed Wt. "^ . \
Fuel H20% Dry 1L.gt~28^/et / g
Fuel: Dry Kg / /„ } % V
A 1 Ao2g §7 B 1
LOADING/TEST START OPERATIONS
Air Settings
Comments
Ave.
Pitot Leak Check
Static
F-SH-7-13
-------
ENGINEERING-SCIENCE, INC.
Client E-iP/'f- Hun »
Date
<£?
ES Projec, f
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charye
Coal Bed 3>, f
Page
Hood Heater Model
Operators
i
CO
I
I
I—'
-p-
Time
Sampl i ng/
Clock
eflio
l SO
i£^
10
iio
I 50
Test
Fuel
Wt.
mil
3,1
fki
S.5
lue
Draft
(in
6.660
C.Ofro
6,030
6 .
Comments
^
_H^
Catalyst Temp
^rc llnternallPost
//(O
XXO
£512-
793
/MS
IICO
ISIS
1/78
/XT. 6
tft
77V
5^
Surface Temp.
Top] Rear] Uottom [Right[Left
33 /
Z70
251.
27 /
277
•29 a,
•287,
-VS7
va/
m
31-7
3/7,
3/^
3/S
£7?
*f
V 3 V
Stack
Temp „
Oil .
Tun.
Temp .
8
_§2_
Room,
Temp.
7/
73
7V
2tL
22.
21
77
97
-------
ENGINEERING-SCIENCE, INC.
Client F/>/9 Run I
Date
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
ES Projec. f ft D-W3 Operators
Page
I
1/1
PC
I
Time
Sampl i ng/
Clock
o5O
1450
ISIO
I'OZ.O
li-lb
Test
uel
Wt.
(Ibs)
•2.,-?
Z.3,
O.(D
•1,7
e.z-
Flue
Draft
(In
H?0)
,020
0.&30
6,0'Si
0.035
0,03(3
0.63C
0,030
Comments
Catalyst Temp
Prc nternal Post
vsy
87?
33^
TL-L.
5&S
•731
"ft?
o $
1*5 /7&
010
ftf'8
Ml
lop Uear Hot torn Right Left
s//
SOZ.
si;
522
Surface Temp.
•3/0
Z&O
^78
•305
•30-7
3/fe
-£30
333
739
33?
337
337
33 S1
-35'J
3-37
'356
36 '2
VZ-/
V67
Stack
Temp .
337
V/v
£22.
on.
Tun.
Temp .
9/
93
93
93
73 -
96
97
97-
33L
99
Room.
Temp.
-7-7
17
•78
7?
So
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client _APjQ Run I .5// - 7
Date /O- 6?- fr r;
ES Projec, f A f) n 3
Wood Heater Model
Operators ft ' /(
Test Fuel Charge
Coal Bed
of ^
A/
i
CO
fa
I
—i
i
Time
Sampl i ng/
Clock
H3Q
'M2-
IS20
Test
Fuel
Wt.
ilkil
O,."?-
Otf)
:lue
Draft
(in
ML
Comments
22JL
7&S
Catalyst Temp
Pre nternal Post
757
873
S57
9/3
71 /
8-SS
79?
79
Top
Surface Temp.
Rear
3o S
•2*3
12.3
Qottoni
3 So
3V/
3VZ.
3V/
^LL.
•3V 7
33S
3/i
Right
3 So
34-X
37
Left
V91
y%7
Stack
35VJ,
3/3
3/2.
337
Oil .
Tun.
Temp .
91
9-7
97
9o
93
-------
J^{ f\r..-A tjiJ--^|-itof
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater /VK-l $
Dati
Sam;
Sam|
Run
2 /6-^- 3»
Pretest Leak Rate d,o$'^JSL ~7"
Post Test Leak Rate ^,^/^/ ^ ?
Meter f • - /(OO7 ty
Read and Record All Data Every IO
\
CO
PC
1
1
t— •
— i
Clock Tune
Sampling (24-hr
time.min Clock)
C\ /(iOO
/o i&to
2o> /C tC
3o /£>3o
c
£0 <(CO
70 ///O
8O l/"2.c3
S 0 //"SO
/OO / HiO
no li^o
/ZO HG&
IjO /7-/O
IVO / 2,2-0
/t>"o /Z3O
/(to /2^o
/70 /2-SC
/^C> /3tf<2
/<7 /3/0
2^0 /'^Z'S'
,7/cP I3'3C'
<£- 'i<3 / 3 V
2-7-5 /'?5CI
~Z-*-S& | LfC(O
930,005
Gas Meter
Reading
(vm) ft3
935.0
9V
^Vi* O
9^O. O
Sf)t> o
•7615,. o —
965", o
_97c)iO
975,o
.c^,o
c?857. 0
*?'^ c* < /
1 <10f:>i ~Z—
1 O / o , "7—
1 OlS^f 1
1 010. 3-
1 o Z-0 • V
i o> z-^". y
( O35, Z.
l oQ
iO 35
'°'^CS
•^Gr3s
.°^S
, <33 5
o o ~? <;'
> r T^
0'>?5
/TOS"
, & ~3*~*,
i c^'B 5
.<^"3 S
/^3S
. ft"^5
/°lb^
-ef>^5
Ori fice Pressure
Differential
( H), in. H?0
Desi red
. ffO
c SO
. >!.o
. FO
, ^^
< ^c5
. KC!
(•&!>
.¥<3
, ^vi'
, Vlj
X %<_-'
. ^o
, ?>^
. "fto
, ^<^
.^•(J
,
, 55,--
^O
« ^°
, ^O
.S'O
.^^
<%o
• %&
• ^o
, tyo
.^6,
Minutes
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
1C -
~7~7 —
4-7
<£ ~
I'i
^7
/t3O
/OCi
/o /
^ /'-
Filter
6 9
•
Impinger
*?<-/
7 "! V *7
~7~\ f-/^
7V
^CJ
*5d
7V S/
/7^"" 's /
7-5 ^5""2_
"7*/
7 ^ ^7^
77 ^S
-7 7 -£"-5
"7-7 ^">
3
-3
v.^
3
rs
">,
-^
~i
^>
^>
•^
3»
^
•^
Flue Draft
in. HoO
-------
^-**i— ^ ^^^vi
Eiim tiszs^
KEE33 \^T^a
ENGINEERING-
o/M'iruinu u/\ i ;\ ^uuni,./ / ^j
V/ood Heater f\ vL--(-$5
SCIENCE, INC.
Date
Sampl i
Sample
/o - <£> " S1 °7
nq Location kT & 2-
Type
Sfe—
) y
Run Number ^/W - 5"6— -"7 A- ^/ "*>
Operator (,-^VXvl > XM^.IS_
i
w
33
1
1
i — •
00
Sampl
time
\ Clock Time
ing\(24-hr
, min^xClock)
.
•zsso i i-t o
•z^,
O (7 ^°
"2.70 i<-f30
1%° m<-/t>
~2ft^> I*-P5C>
'^&Cy 1 $£>O
^~\ 1 ^ / *5 /"^^
_5 2 O 1 "t~y £0
3 30 / 5 jo
3^0 15*/o
>£? i^5C>
^o ,6,06
3 70 (u>° (&,fO
'-iiO /6.5'D
fzo < 7
*~/ *~? O / "7 "^ ^
Gas Mater
Readi ng
(Vm) ft3
/ 046.0
; C) 7<^>.^
/ 07S.O
1 -J80 . 0 _
1 085.0
j_ 690.0
1 (J^^O
( / &O a 1
1 / £? 5"# /
i //o.o-
i/2orf o
( / 7,<^tf C)
/ f^O-f O
/ /55"« /
ilVot /-
/ /VS. -2.
l/ftp. -2.
, / ^,^j „, ^
i /^_5 o y
Velocity
Head
(APS) in.
H?0
<9.o 3 S
<5(o3 5
0 -o -3 5
Q ,012)3
0.03 S
^.o^S
0< o 3S
6.ci3 5
<9cC->3S
O , O"?,^
a a 3S
^ <-
b ^ 3^
"7 CT"
. ^ ^^
» 35"
^^-35
^^ 3 5
^ ^, -2, <^
o <2> "5 5
Orifice Pressure
Differential
(AH), -in. H?0
Desi red
, ^
. £o
•yo
. 5^o
c %&
. ^o
,»o
. ^
, ^L)
' 15 o
- "Jo
' &0
f t><^>
j £>a
' ^ £>
a ^O
•o ft£>
t> S>£>
- ?5 c>
„ 5^3
> 5o
« be)
/ s
. So
' S^1
- F, o
x
- So
, f)£;
„ ^^p
'•^o
,55,5,
, go
, fS<^>
• ^t9
. S ^
TEMPERATURES
Dilution
Tunnel
..
Meter
In
-
Meter
Out
/A/
/o/
/O^L
/O ^_-
/O 5_
/^"Z--
/o ~z_
i-ti ^_
/^ 2_
//7 ^
/ ^5 2_
/O 1 -
/<5 2_
/<^3
/ ^ J
/
fat/
So*/
/&¥
/ & "^
Filter
S/
6Y
6? ^
S'S-
©~z_
;?
8,3
"^ "3
8 3
ft "?•
% 3
"S Z
Impinger
5-Cp
S"7
^""7
S-'T
5-7
S"-/
^ "7
5
^3
"^
.3
j?
Flue Draft
in. H?0
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
lo-fr-
Sampling Location
Sample Type -Z, ft /
Run Number ~ f
Operator
\. Clock Time
Sampling\(24-hr
time, minXfylock)
*~Z/7S -H5£___
tjfto f4,-T>O /^^o
^Vn I°lc0
^O f °l /O
56>0 14 to
9 go /5. 2-
/l-lo, -2_
/•2/5- /
/7_20, /
/ 2.-Z.^-2/S=
•2,^^2./7_
Velocity
Head
UPS) in.
H?0
- />•* <;
j o -^ <5~
* <$
rO^>5
.n -*> 5
* 3^
. tf 35"
Orifice Pressure
Differential
(AH), -in. H?0
Desi red
Actual
*ftQ
*f60
<• KG
* t>0
o %0
- Ko
d &C>
/» ?• '"-1
^ ^
'9?
^ ?
9^
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number_
Operator
Start Time
Stop Time
Ys~T~-
Ambient Temperature
Barometric Pressure
Static Pressure, (P«
Filter Number(s)
Meter
Probe Length and Type_
Pi tot Tube Coefficient_
Assumed Moisture
Sample Box Number
Meter Box Number
Meter H
Pretest Leak Rate
Post Test Leak Rate
Read and Record All Data Every ID Minutes
Sampling
time.mln
Clock Time
(24-hr
Clock)
150,00 "L.
Gas Meter
Reading
aa-itL
Veloci ty
Head
( PS),in,
H_2_°
Orifice Pressure
Di fferential
( H), In. H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter!Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. HoO
•• *• •
o.e1 3 S
_7_0_
/35.o
7.0
,•7-5
•7ft
,95
-7V
VC
/eve
. o
^_
, 0
6,0 3 S
-75
/CO
T; -
1(10
ASS.rn
"77
.95
3&.
,95
J77_
77
97
-Z2L
/ZC
7
-. o
2-50,
y
^og. ^
9ft
I
CO
PS
I
ho
O
,035
55
.7-5
J2.
•2
3 -
50
ZZ.5"
-3
lrr
S/
.0-3
•^35.
So
1^5. O
. O — 1 - o "3
-------
'•gra
HTJ3 I
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cpnt.)
Wood Heater
Date ~
Sampling Location
Sample Type
Run Number
Operator l^
Clock Time
Sampling\(24-hr
time, min\£lock)
Gas Mater
Reading
. 0
Veloci ty
Head
UPS) in
H?0
Orifice Pressure
Differential
(AH), -in. ll?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H20
Z-0
. 0
,95'
82-
2-
^"35-
. o
2,10
.63 S
9s
-TV
285, 0
5*7
.035
±5L
j^L
JS_3_
/w
-^ T
ST3
'78°
95
•2.
-.3^
"2,
•a 0
-95-
"7
1130
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood lleater_
Date u -
Sampling Location
Sample Type 7 % y
Run Number ~5/V x - 7 /3
Operator
3/3
^\^ Clock Time
Sampling\(24-hr
time, min^xClock)
~V~~?"ZT~~ — " — t2-£-£^_
-V # D /•<&&&
H^o Ifi Jo
^av H to
S/rt 1-b -*>&
^5o t(.^n
^-Ip /t><=>o
?Vc> l^ 00
*=> 5~o fct /n_
5& IQ-ZO
^•7n /Q 10
S "S 0 / 69. cl'
37V. ^
"5^^- 5
-^ Vo 9
3 S-?. 'T
3^?T
*?S
09S
^ 95
• ?5~
-?^
;95
TEMPERATURES
Di lution
Tunnel
/
1-
•*ls
97.^
Meter
In
-
Meter
Out
/PV-
/^3
/^>
/ &'i-
/& ~L,
/C- 7-
fa' ~
/ -
W.o
Filter
ft/
to
Ka
So
<&0
•ko
-7^
«
Impinger
S^
5"^
5^
?C
s 6
s <^.
s->
57
^7
S7
57
S7
•
Pump
Vacuum
in. Hg
-?
>
-z .
7_
7_
2^
1_
T_
"t.
T.
-?
Flue Draft
in. H?0
Tl
I
CO
Pd
I
i
to
to
-------
FUEL MEASUREMENTS
Date/O"& "^^ Wood Heater Manufacturer
Project No. £_D>/2,'~\
Run No. <,M - 7
,*r*~~ ^'
Circle One: (grg^PstJ^I
Fuel Type and Amount 2x4
Ideal Load Weight
Wood" Heater Model ft V- 1 &>
. Test Fuel
\s^ 4x4 1x4
.Actual Load Weight
Fuel Piece Length ^
-------
FUEL MEASUREMENTS
Date jb-£ '^^7 Wood Heater Manufacturer
Project No. Afifz^ Wood" Heater Model_
Run No. ^(4-^7
Circle One: Pretest Fuel T«
Fuel Type and Amount 2x4 2— 4x4 ~2_ 1x4
Ideal Load Weight ' _.Actual Load Weight_ "
Fuel Piece Length_ i ~?
Moisture Meter Calibration 12% (i_ 225 2_"V-
•il
'\^Z-
VS^
'r,b*1
ZXV5
Moisture Content- (Meter - Dry Basi$)-Co'v*c7't J 1(1 y^ / "^ ^^ " t*'
3 Z_J|7 Z.^-\. 2^/, ^ "Z^ ^, ?o
4 z^6 10. V ^,n ^3./7
r
6 2'3.o eai ^o.<; -Z_/,zo
jJ
y Z.Z.I 15, j 3Z,<3 1^2,0 ~T-,3-
-------
TEST
SH-8
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: SWEET HOME
Model no: RK-18
Lab name: ES
1st date: 10-9-89
Run no : SH-5G-8R
1st time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
2-10
300
360
420
480
540
550
550.00
Units l^metric,
2-English:
Y, DGM:
Pi tot co:
Gas
Pb (mm, in.
Stack area (m2,
Wood moist (7.
25.90
vel dp
(mm H20)
(in.H20)
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
stack
temp
(C,F)
82
82
81
79
84
88
82
80
86
85
84
OGM
rdg
(m3,ft3)
225.000
254.600
284.900
314.600
344.400
374.500
404.900
434.800
464.700
494.700
499.735
MW :
Hq):
ft2):
wet):
Burn
DGM
temp
(C,F)
65
81
84
85
91
95
85
84
90
94
94
2
1.007
0.99
28.56
29.94
0. 1963
18.83
rate (dry
DGM dH
(mm H20)
(in.H20)
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
0.800
Samp vol
(sm3,scf)
268.853
85.49
17.640
Flou rate
(dsm3m
kg/hr):
vel
(m/min)
(ft/min)
788.11
788.11
787.39
785.93
789.57
792.46
788.11
786.66
791.02
790.29
789.57
,dscfm)
144.59
1.04
PR
(2)
102.3
101.5
98.6
99.9
100.1
98.9
99.2
100.7
99.2
99.1
dDGM
vol std
(n»3,ft3)
30.044
29.845
29.093
29. 137
29.110
29. 189
29.235
29.289
29.066
4.843
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
788.84
(C,F)
83.00
i
CO
EC
I
OO
I
-------
Method 56 Proportionality Rate, Flow Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
Tst time
(min):
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
210
300
360
420
480
540
550
StEET HOME Units l=metric,
RK-18 2=English:
ES Y, 06M:
10-9-89 Pi tot co:
SH-56-8B Gas MM :
Pb (mm, in. Hg):
550.00 Stack area (m2,ft2):
Mood moist (.'/. uet):
25.90 Burn
vel dp
(mm H20)
(in.H20)
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
stack
temp
(C,F)
82
82
81
79
84
88
82
80
86
85
84
(m3
425
454
484
514
544
574
604
633
664
694
699
D6M
rdq
,ft3)
.001
.600
.900
.600
.300
.500
.200
.900
.300
.700
.714
DGM
temp
(C,F)
64
84
89
89
91
96
90
89
91
94
94
Samp vol
2 (sm3,scf)
1.024 272.235
0.99
28.56 Flou rate
29.94 (dsn>3m,dscfm)
0.1963 144.59
18.83
rate (dry kg/hr): 1.04
DGM dH
(mm H20)
(in.H20)
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
vel
(m/min)
(ft/min)
788.11
788.11
787.39
785.93
789.57
792.46
788.11
786.66
791.02
790.29
789.57
PR
(*)
103.0
101.4
98.2
99.3
100.9
96.9
98.1
10L9
100.8
99.1
85.49
17.640
460.00
1850.00
dOGM
vol
(m3,
30.
30.
29.
29.
29.
28.
29.
30.
29.
4.
std
ft3)
620
193
326
326
711
956
272
017
908
906
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
788.84 83.00
i
CO
PC
I
oo
I
ro
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED
DATE RETRIEVED
TEST LOCATION^
SAMPLER SNtf 1
(HG BAROMETER
PRETEST B.P"!^
TANK 19, 9 CP
TORR ABSOLUTE
POSTTEST B.P. '
TANK /<£. 7. S
TORR ABSOLUTE
/0-7-Z1
P5-^ 5-^*1.
,V/£9
UNCORRECTED)
1.^7 (IN HG)
(—IN HG)
7.*
3^.<*v (IN
(—IN HG)
^5o,3
PROBE /, /
LINE / . Cj
CONDENSATE b> . £
£L- FILTER^l A (/
FILTER//2 - O . 3
TOTAL (MG) -S.l
TEMP. ;q (c)
HG)
TEMP- 7_T_ (C)
RUN*
Itbi lint ^ >
STOVE ID /5/<-
WOOD SPECIES_£
WOOD MOISTURE
WUUU MOISTURE
WOOD CONSUMED
S//-VP
'£ (MIN.
/ (J
Jo<*. a\ /X? 5
(Z DRY) Z.'
T-^/9
) ^,^7^
/^;
5.*-0
(% WET) / c • 9 ^
(LB) ^'^
(KG) l(Vti
SAMPLE FLOW RATE PRETEST
ROTSHETER ^ , / (IN H-20 MIN)
START S. / (IN H20) FINAL $.0 (IN H2) LEAK RATE C . / (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
C0(2) L
C . / C '
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE+FITTING
SAMPLE LINE
CONNECTOR
MIN.
MIN.
MIN-
DELTA
F-SH-8-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED /O ~ 9 - 8
DATE RETRIEVED
TEST LOCATION £
SAMPLER
(HG BAROMETER UNCORRECTED)
PRETEST B.P?9,
-------
CLIENT ,
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page of_:
I
RUN No. <^H~(}PJ'-<5^ Placed in Dessicator: Date/Time_/£rZo.
STOVE MODEL No.
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
Its- II - V\
1 o "ho
lo-n- s^
/ (e 1 0
'
9-/7-S^
'
FRONT
RTr.TKR II
$4£-tt
. /-Z-/7
•tT-)1
, ii/ 0 3
CALIBRATION WT.
WT AMOUNT =
PRE WT
• ^~>f>O(J
« ^oo /
POST WT.
. /
. $oad
ROOM CONDITIONS
RELATIVE
HUMIDITY
yy <^<^7
v^©^^
BAROMTRC
PRESSURE
Z9-95
7.9- ^S^
Initials
l
/*<•%
frt£
i
CO
33
I
OO
I
Ln
(A)
.(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of
CLIENT
RUH No. , «<=>
16 - II
to - il-
1 *3 1 O
•
9-/S-89
POSTEST Acetone Sample Volume
REARER It
/)-S9
77.97/7
19. cl~>o^
-77.970-?
77,97otf .
0,oo$0
CALIBRATION WT
WT AMOUNT =
PRE WT
^6,0*00
n o t tjfjqCs
£> '6 • 6 o 0 /
POST WT
^o *&o& "Z--
ij Cj x '7<9•?
ROOM CONDITIONS
RELATIVE
HUMIDITY
vy^7'
^Q>^
^5^7/
BAROMTRC
PRESSURE
Z9.9S
'z9. ^7
•z-9'?L
9 r
Initials
/»*4
^.£
i
GO
1
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
O
D,
(C)
TOTAL PARTICIPATE CATCH (A+E+C) =.
. oo o
-------
CLIENT .£ P A
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. S/A^lr-ff/3 Placed in Dess icator: Date/Time.
ES PROJECT .ftD/1'b
STOVE MODEL No. /?/<-/
POSTEST
1 WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
jo -If
\o -^)
lo - »
Iff 7.0
9-/7-S?
FRONT
PTr.TRH It
Sj£-&/
*lt.lD
. /T-T-C'
* /Z?.^
- /t-Lf
0,CrfO G
BACK
FTf.TRR II
54^-61-
. /"Z-O?
« /t-C>
. ^cny/
POST WT.
. 4<» /
. 5 000
ROOM CONDITIONS
RELATIVE
HUMIDITY
V/^%7
V^@*7/
BAROMTRC
PRESSURE
•Z^?-95
^9- 9^
Initials
,
/^ic^
/^ic^
I
CO
ffi
I
00
I
(A)
(B)
-------
CLIENT
ES PROJECT RD S23
PARTIGULATE WEIGHTS SUMMARY Page of.
RUN No. 5ft-lift-*&(*> Placed in Dessicator: Date/Time.
STOVE MODEL No.
POGTEST
Acetone Lot \\ <3/ /
Acetone Sample Volume.
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
jo- //
to- If
lo - 1~L
i <=> 1 ^
^-n-v)
-r~tf
BEAKER it
7SJV93
-7£./VKtf
7 % . /5
CALIBRATION WT
WT AMOUNT
PRE WT
^-> £> • £>C>() O
U G Q Q QQ
^0 . OOC I
-
POST WT
*} & t &0& °^-~
¥?.e?e^^
So. oco/
ROOM CONDITIONS
RELATIVE
HUMIDITY
Vy(£^/
v#3k
i
CO
pa
i
oo
I
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(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
O
O .
5 _
TOTAL PARTICULATE CATCH (A+B+C) =.
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT
ES PROJECT AO
RUN No. SH-56-84 Placed in Dessicator: Date/Time
»
STOVE MODEL No.
POSTEST
Acetone Lot U 9// &
Acetone Sample Volume (f> I
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
r
TARE WT
NET
DATE /TIME
If -It
Hot
to - If
!(,<;<=,
10-11,
) ^ ~Lo
9-/S-^9
BEAKER 11
fi-b?
7%. 3>?7?
7fJ . 3V90
7«. -?V9^
-7*.3
29.
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN Mo. <5M-£>G~e&A Placed in Dessicator: Date/Time,/^
ES PROJECT R D / 2 3
STOVE MODEL No. X? M ~
POSTEST
WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
lo-t/
t^> lOln
lo- >/
I Z 16
\o -
9-X7-3?
FRONT
FTF.TER 11
A£- $5
,C,q$3
*6^#
,w&
,676'3
(D. 0/f)^
BACK
I'Tr.TRR It
/9^"53^
. (fl 9 Z 6
^^f.t?..
.65J7£
,6^^^
errO^(f>
CALIBRATION WT.
WT AMOUNT =
PRE WT
«. ^OCi O
f 5^^ 1.
POST WT
. //??
I
CO
33
I
GO
I
(A)
(B)
-------
CLIENT
ES PROJECT /? O
PARTICULATE WEIGHTS SUMMARY ' Page of.
RUN No. $/V- 5(fr-ft/? Placed in Dessicator: Date/Time /(T &
I
STOVE MODEL No. A'K-
POSTEST
Acetone Lot It
Acetone Sample Volume /7
WT 1
WT 2 .
WT 3
WT 4 >
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
\0~ //
//,$£•,
1 0 - 1 1—
9^-89
REAKER 11
^^^
M^/?
/H^
I
Crt
EC
I
CO
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
0}
(C)
TOTAL PARTICULATE CATCH (A+Bn-C) =.
-------
CLIENT ,
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. 5/V .-.££-% /£ Placed in Dessicator: Date/Time.
STOVE MODEL No.
PO'STEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
\o-il
lo to
la -//
/•5-3S"
d>O
. ^/
POST WT
.4/99^
r
-------
Client _
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
, •
ES Project i
/ 2,
"Wood Heater Model
Operators Vo
-( 6
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr)
Achieved Burn Rate (Kg/hr)
Primary Air Setting "2-o
Secondary Air Setting MA-
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
Pretest
C>
Post Test
-7
TEST FUEL DATA
Firebox Volume (ft-)
Fuel Charge Range Wt.tj-»C? to
Actual Fuel Charge Wt.'^_}_
Coal Bed Range Wt.?,7 to 3.
Actual Coal Bed Wt. '3>-.O
Fuel H20% Dry 'Z-3i,ZoWet /
Fuel: Dry Kg 7/53 -ba-4j Air Settings
Door 6&j.r\ <• \VXc- Comments
Veloci ty Traverse
2
3 0,i
4
Ave.
Pitot Leak Check
Static
F-SH-8-13
-------
WOOD HEATER CEHTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINL: ^RING-SCIENCE, INC.
Client t? ft ft- _ Run I
~ &
Date
Hood Heater Model
Test Fuel Charge
Coal Qed *?>. O
Page / of 3
ES Projec, I
Operators
A!
PC
I
CD
I
Time
Sanipl i ng/
Clock
0^-2.0
/O/O
/ozo
IOHO
(|l-0
I'-JO
Test
Fuel
Wt.
(Ibs)
-S4-
ue
Draft
(In
HpO)
0,060
690
-i^t> /)
Comments
T/C
-6
Catalyst Temp
in:-,
571
851
nternal Post
RM
-112-
in-
3.
|I61
lop
/77
'iif
Y.S
Rear
Surface Temp.
6 /
Wi-
'ft I
Uottom
7560
•20 /
TOT
S/fl
Hi 3
212.
:v?
Left
7 £
667
(:-<-/
vvfr
VV "-/
^61
"S7T
53
£?/
_ZL
7?
B/
65'
6$
70
7o
Ai
-------
ENGINEERING-SCIENCE, INC.
Client. '
Date
ES Projec, f
HOOD IIEATEK CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Wood Heater Model
Operators V
Page
of
-i B Coal Bed
I
oo
I
Time
Sampling/
Clock
/T,tO
LLT-O
!^H(?
Test
Fuel
Wt.
(Ibs)
2.0
I.-7
/.V
1,0
iza.
lue
Draft
(In
H?0)
0,
Q
Comments
Catalyst Temp
(- llnternal Post
052.
335.
77*5
512
/CIS
//•*>?
75"?
97^
><\r<
Top
r
VO
v
7Z-
69
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
Date
Sampling Location
Sample Type
Run Number C, (.
Operator y^U1
KT
- ^ 6- - 5* A
A
•3/3
\. Clock Time
Sampling\(24-hr
time, min^xClock)
~ • — —_
V8o H6o
H°L^ iS<=-^
6^C> I'Sto
5/0 C&2^>
5^ /S^3-o
53o 'Byo
5Vo /S5o
55o no<>
*;^
Gas Hater
Reading
(vm) ft3
*y6*y. 7
^&^. ^
V7V.-7
Hl%~f
HS^^-l
ye?. -7
v^v,7
VH.73^
•2.7^7?^
Veloci ty
' Head
UPS) in.
HP0
,^^^
.^3^
.e-l.'gr
• 61>^
.0-3 S'
.o-S*
. o -^ -^r
.0^^
./,-5V
Ori f ice Pressure
Oi f ferential
(A II), -in. H?0
Desi red
,%o
. SO
,^o
, ^
,«?o
' . KO
.•»o
.^
Actual
,t$c=
> C60
. 30
.fctt
,30
. go
.'dio
.^0
,9^>
TEMPERATURES
Dilution
Tunnel
I,
V
^^/^^-
"^
Meter
In
-
Meter
Out
9c>
^^
C?1L
91
^3
9y
9V
9V
«^fr«
^^r^
Filter
7/
•72-
7-3
7^
7-^
-73
73
73
Impinger
^T
f?Q
£-C^
5"ci
-5G
S"^
S'~7
5-7
•
'ump
Vacuum
in. Hg
"i
•^
"3
3
?>
3
•^
"^
Flue Draft
in. H?0
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type
Run Number
Ope rato r
33T
Start Time
Stop Time
Ambient Temperature
Barometric Press'ure
Static Pressure, (P~$T_
Filter Number(s) "
Meter -,
Probe Length and Type_
Pi tot Tube Coefficient^
Assumed Moisture
Sample Box Number
Meter Box Number
Meter H
~f
'/
Pretest Leak Rate
Post Test Leak Rate 7^7
s-o
^L
5" "?>
no.
.6 T>fi
S'o
• Sto
3 Ci
. Ko
^L2_
L2_
15-0
. Zo
//?.<=>
.tfo
8-S
'X
100
'no
\oi-z
'b
// yi>
0
67
II5Q
50
67
rs
ci»
I
CO
PC
I
oo
I
v?
0-7
3-0
7s
G.
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood Heater
Date
/
__ ______
Sampling Location
Sample Type -2.
Run Number
Qperator
5
.
5 fy < -
Sampl i ng
time,
Clock Time
24-hr
Gas Mater
Readi nq
V ft
Veloci ty
Head
H?0
Ori f ice Pressure
Di f ferenti al
(All), -in. ll?0
Desi red
Actual
TEMPERATURES
Jilution
Tunnel
Meter
In
Meter
Out
Filter
Impinge'r
3
'ump
Vacuum
in. Hg
Flue Draft
in. H20
V
73
7-
IH <5o
7?
5
z
39?.
-2=2.
•5"?
7
_.£fifi.
2-.
•7 .
SL
, tf o
6-7
/ 7
.8-0
6-7
I
CO
PC
I
OO
I
_X
-7
"70
-------
E/3233 /IF2*"*
t._!-.-rrr» tiUETO .
tgrrn-'J
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood lleater_
Date
-(o
Sainpling Location KT
Sample Type
Run Number c^
.Operator v/oUll y
A
3/3
• ' \. Clock Time
S amp l1ngX.(2 4-hr
time, nnn^vQlock)
• — — _
Y8o n<3o
52c^ /S^o
53o «8Vo
5Vo /&5o
550 H0i>
^^
Gas Hater
Readi nq
(Vm) ft3
Vb'i, J
^fp°l. (f
^7^-7
^~Ti.~j
VSH.^f
ye?. ~i
V?V-7
V^.TSS
•Z7y,73<
Veloci ty
Head
UPS) in.
H90
./^^^
,o3*
ic.'i'gr
.61,^
-^•^^
,0-3^
. c> :? -gr
..o?.^
.*-3V
Ori f ice Pressure
Di f ferenti al
(All), -in. H?0
Desired
,#>.
. So
.^0
> eft.
r«iro
• . KV
.•rfo
,^j
Actual
, ^^
.-bo
. 8 0
. fcta
-30
- 80
.'<^o
.^0
,9^
TEMPERATURES
Di lution
Tunnel
|.
V
%\fo1.
v }t " •--
Meter
In
-
Meter
Out
y
9V
^/V
*^-frrt
-------
ENGINEERING-SCIENCE, INC.
SAMPLING OATA
Wood Heater f> \{ AlC-io.
Date
Samp
fd>. Cf - £V-t
ling Location j^ #"^
Sample Type fA>r><^ v
Run
Number S H- - ??> ( &H -'TJ <-r - S ^>
Start Time
Stop Time
Probe Length and
Pitot Tube Coeffi
\ Assumed Moisture
Operator ^\V , ^ r\< l/\
Ambient Temper
Barometric Pre
Static Pressur
Filter Numberl
Meter 1
atur'e
;ssure
e, (Pq)
s)
O-Li-l
0950
/'foo
lype . /^"
cient , cy^
V
Sample Box Number
Meter Box
Meter H
Number
USS - /
Pretest Leak Rate .to1-/ C2, /o "
Post Test Leak Rate /^oS on-? /o •/
Read and Record All Data Every /O Minutes
i
CO
PC
1
OO
1
Ni
0
Clock Time
Sampling (24-hr
time.min Clock)
£> &cl 1? O
/O /<9 C» O
2^0 /O / o
^O (02.^ '
V^1 1 OT C*
5e> /ovo
4.0 /<35-O
•70 / /^cr>
S'O //(O
9e> il La
/If ll^O
/ifc> //so
ti{£> 1 ? ) O
15° iz,"2C3
frjo /zi&
,<£> /Z5o
1*70 (&>&
?x> /3/G
••IP /-?>->o
->t-o /7^,c>
v> °o /">«-/ o
1 .'. -/o /-3ITC^
Gas Meter
Readi ng
(Vm) ffc3
^£•7.9
^3^. 8
^/?9. "7
VW, ^
^yy?/ 6
^S^.,4.
£/£'{/. ^
"y&H \ ~~1
^/%9, 7
-/7iy( -?
/y--^ £
5 T> s-/- S
5 "^> "9 *• S"
.-5- -?^4<. "Si
veloci ty
Head
( PS), in.
H20
A03&
c-.oT5>
6.0 T> •£>
0«^\
<&^&
.,&1( ¥
,or?&>
f o '3 £>
i ^'3 '^
/ 033
• o^i^
.03^0
.CG.'j
, o 3 &• •
\Ct~~>'y
o'bS'
, o 3 ^
<3 "TS^
6 <1 "^ 'K"
Orifice f
Differe
( H), in.
Desi red
» 9'~>
< cr*i
.9S
,'75
• c/c>
^9^
, 9'S
. C/S
, V^
c°) "S
, "~i ^
.^•3
.95
• '/'S
' 1>S
f ri"s
. r? ^
. 'I'r-j
. ^"ri
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. '^
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^«-3fe' >*7S-
ressure
•ntial
H20
Actual
,75
,"/ ^S
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. 9 5
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. "7 .'S
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. ^S
i0/ •j,
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i '?S
- ^5'
.9s,
•• ''S
. f>^
.9s
. ^ "5
•^S
i*? 'S
-^ 5
" ^--^
"^ -7
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
GY
(P i~t
•73
#t»
3z_
&<-/
*i>Lf
B^7
&> ^>
f^0/
<^ y
Filter
6 ~7
'Af^-e /^7
Impi nger
r^ t-/ •
/^^ c^^)
6 ?s ^y /
<£&, '//
^ ^ ^-/t>
Co fr ^^
61
«//
y4
7 2— V"7
77 V7
7o V6
7>
3
3
"^
~>,
•T,
-v^
^— ^ — '
-.?
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater /) M -
Date }Q - •? - S^
Sampling Location £~_"?-
Sample Type
Run Number__
Operator /y(
Sampl 1
time,
Clock Time
x^A-hr
min^v£lock)
Gas Mater
Readi ng
) ft3
Velocity
Head
0.
3ri fice Pressure
Di fferenti al
. M?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Muter
Out
Fi1terIImpinger
Vacuum
in. Hg
Flue Draft
in. H?0
7
•2-50
o,
0
T
76
_S
J7J2.
_2
o .e'2,*
3-L
.0 .(J>
&
-79
7-2
_51
^4^ r
£> ?.
3 1S
„ Q
6, *-*><%
/^"?P
ID
70
5b
^3L
so
I
CO
PC
I
00
I
to
^IK.
5o
12,
?
-------
jmmn/ffinsa
§1=123 tS-iSSs
L'j'T? ir*.
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood lleater_
Date
Sampling Location
Sample Type
Run Number
Operator (
-9-8*7
T>T
nl-
\. Clock Time
Sampl i ng\(24-hr
time, min^xClock)
"~ - — - — — -— , __
Vfto iT^'o
ij'a/£> I 8>oo
fyx> 1 ft 10
"3/0 /S-2-o
6^° r£>7°
S T> O / f) V £>
5 c/o 1 8 So
GSO l°fC>&
c, ^&
Gas Mater
Readi ng
(vm) ft3
6-6 9, "^
Ct?~iH- ^1
6 "7 9. ^
^fL^L^k
^ g>9. "7
£ 9 V. 7
69^.7) ^
"2»7/, 7/3
Veloci ty
Head
UPS) in.
H?0
^7>^
.c>3ir
,63i^
' C1 '*> c&
.0?) ^
.^ "3 2^
,0 "^ ^
,^"3>S
.ȣ) "z.^
Ori f ice Pressure
Di f ferenti al
(All), -in. ll?0
Desi red
.c/s
.^S
. 9s
- '} ')
.95
' «c/5
i / -^
, 9 ^
Actual
. c,s
•9S
. V^
- 5'5
. 9^
.95
i • 7>
,9-S
, G^
'
TEMPERATURES
Di lution
Tunnel
J'
V
q -^ .^T.
Meter
In
-
Meter
Out
S/
9 3
9^
?Y
^t-/
9V
U^*^<
Filter
-7V
7*>"
76
74-
/ d^
/ J<>
Impinger
sv
5 i_
5' ^_
5 i-
5" -^
•5""S
5"\
•
Dump
Vacuum
in. Hg
~~Z-
~z.
2
~2_
^_
^_
7_
^_ •
Flue Draft
in. H?0
EC
I
c»
I
-------
FUEL MEASUREMENTS
Date /fl-*/- ^°? Wood Heater Manufacturer
Project No. ft fSf £ "=*=?> Wood" Heater Model
Run No. <=; u. — C7
-
Circle One: (?rete^tj^r ^- Test Fuel
Fuel Type and Amount — 2x4 ^^ 4x4 1x4
Ideal Load Weight ; .Actual Load Weight ~
Fuel Piece"Length
Moisture Meter Calibration 12i ±r%Jt>_L 22>
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Piece No. Readings Average
1 ^ 2V,3
Overall Fuel Moisture Average
F-SH-8-23
-------
Date
Project No.
Run No.
Fuel Piece Length
FUEL MEASUREMENTS
16-^1 - 8 °1
Wood Heater Manufacturer
Wood" Heater Model
Circle One: Pretest Fuel _ <[«tjj.
Fuel Type and Amount 2x4 'Z^-~ 4x4 ~? ^ 1x4
Ideal Load Weight ; .Actual Load "weight "
(."
Moisture Meter Calibration 12%
22>
Moisture Content- (Meter - Dry Basis)-Co|rV1*:c'?"t
-------
APPENDIX G
PROPORTIONALITY DATA AND ALL RAW RUN DATA
FOR EACH CC-150 TEST AT RESEARCH TRIANGLE PARK
5\W>123.40
MD8LUPP
-------
TEST
CC5-1
"S\RD123.40
-------
o
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
Tst date: 9-21-89
Run no : CC5-56-1H
Tst time
(min): 577.00
Chrg ut
(Ib uet): 30.10
run
time
(min)
0
60
120
180
240
300
360
420
480
540
577
vel dp
(mm H20)
(in.H20)
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
Units 1-metric,
2=Engl ish:
Y, DGM:
Pitot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.?. uet):
Burn
stack
temp
(C,F)
%
101
99
96
95
104
97
94
102
94
91
0
iGM
rdg
(m3,
751.
782.
814.
846.
878.
909.
941.
973.
1005.
1037.
1057.
ft3)
002
600
300
000
100
800
600
500
400
300
031
DGM
temp
(C,F)
82
90
93
95
93
93
93
94
91
90
90
Samp vol
2 (sm3,scf)
0.995 290.277
0.99
28.56 Flou rate
29.74 (dsm3m,dscfm)
0.1963 138.46
17.76
rate (dry kg/hr): 1.17
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
779.54
783.04
781.64
779.54
778.84
785. 13
780.25
778. 14
783.74
778.14
776.03
PR
CM
101.8
99.9
99.0
99.9
100.7
99.0
99.4
100.9
99.3
100.0
dDGM
vol std
(m3,ft3)
30.494
30. 147
29.984
30.253
29.984
30.078
30. 173
30.118
30.282
18.764
8'5.49
17.640
460.00
1850.00
vs/VmTs
.00
!
vs ave stack
ave temp
(C,F)
780.37 97.18
o
r>
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
1st date:
Run no :
1st time
(min):
Chrg wt
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
540
577
ORVILLE
CC150'
ES
9-21-89
CC5-56-1B
577.00
30.10
vel dp
(mm H20)
(in.H20)
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
Units l^metric,
2=English:
Y, DGM:
Pi tot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist C/. uet):
Burn
stack
temp
(C,F)
%
101
99
96
95
104
97
94
102
94
91
OGM
rdg
(m3,
743.
773.
804.
836.
867.
898.
930.
962.
993.
1024.
1044.
ft3)
201
800
900
200
TOO
900
500
900
500
900
528
DGM
temp
CC,F>
82
90
94
95
94
93
93
91
90
90
89
Samp vol
2 (sm3,scf)
1.009 290.025
0.99
28.56 Flou rate
29.74 (dsm3m,dscfm)
0.1963 138.46
17.76
rate (dry kg/hr): 1.17
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
779.54
783.04
781.64
779.54
778.84
785. 13
780.25
778.14
783.74
778. 14
776.03
PR
(.?.)
100.1
99.5
99.0
99.6
100.5
99.9
102.5
98.8
99.4
101.0
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
29.
30.
29.
30.
29.
30.
31.
29.
30.
18.
std vs/VmTs
ft3)
954 .00
002
977
114
881
319
086
466
291
935
vs ave stack
ave temp
(C,F)
780.37 97.18
o
i
o
o
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED
~8 *7
DATE RETRIEVED 9- 1.7. . g *?
TEST LOCATION £~5 4J 5> <£/»£>
SAMPLER SN# 9 6 7. 3 V
(HG BAROMETER UNCORRECTED)
PRETEST B.PZ9-9Z (IN HG)
TANK 29. SO (--IN HG)
TORR ABSOLUTE
POSTTEST B.P. , 7_Q. _
IN HG)
WEIGHT GAINS
PROBE
LINE
CONDENSATE
FILTER//1
FILTER//2
7.
TOTAL (MG) V9. 3
TANK
.TORR ABSOLUTE
(—IN HG) TEMP . "2. /
$, Q
(C)
RUN,?
- /
TEST TIME f 7 7 (MIN . )
STOVE ID
WOOD SPECIES
e Hi V
WOOD MOISTURE (% DRY) 2./. 5" 9
WOOD MOISTURE (% WET) / ?, 7 <»
WOOD CONSUMED (LB) 3 .'
POSTTEST LEAK CHECK
STARTS. 9 (IN H20) FINAL 6, 7 (IN H2) LEAK RATE £^-2- (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS :
A f f/
C02(%)
/*>,
'
4 ft
oz(%)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
/JL M I N .
jr?<
PROBEs-FITTING
SAMPLE LINE
CONNECTOR
. 612 S 3Y-6779
G-CC5-1-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
DATE DEPLOYED 9-2/-S9
DATE RETRIEVED q - 1 2 - $ / (IN H20) LEAK RATE <3, ~) (IN H20 MIN)
POSTTEST LEAK CHECK
START 5, ^ (IN H20) FINAL £
_(IN H2) LEAK RATE ^ . % (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(%)
RUN COMMENTS: 7^1/
f /
O K
C0(%)
02(%)
/ -7
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN-
MIN.
MIN.
MIN. DELTA
PROBE+FITTING
SAMPLE LINE 3(o•
CONNECTOR
G-CC5-1-4
-------
CLIENT
ES PROJECT ]£.
PARTICULATE WEIGHTS SUMMARY Page / of /
RUN No.iTrC- 53-•//?. Placed in Dessicator: Date/Time_^Zlll5.
STOVE MODEL Mo. CC /
POSTEST
, ' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
'9--2LV
05VS
<5 - 1 5
//> -2. C
n
°i-n
FRONT
FILTER It
SAZ-I
•/39/
*/ ^?^
-/^^^
«/389
» ^Z/3
^5 .<3 /7^
BACK
FILTER t(
5^-2
- yz/'?
o /-2- / y
a/2.7<-
- ^ /(<.
* y^z/6
• ^
CALIBRATION WT.
WT AMOUNT -
PRE WT
" c/99ci
0 r>f>ot-
* ^v-o-o
POST WT
a 5 '-'£•/,
- V99*)
* ^oo /
ROOM CONDITIONS
RELATIVE
HUMIDITY
^•^\£
yM^
W&tf
BAROMTRC
PRESSURE
•z.9,96
^,
•2.9.f S'
2 9. S 5
Initials
(
totC %
/•vi ^ >p
/^c^
1
I
o
o
(A)
(B)
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of.
RUN No. CCS-UPT^/ft Placed in Dessicator: Date/Time.
ES PROJECT RD /"*• 3
STOVE MODEL No. CC.-/S'Q
POSTEST
Acetone Lot \\ 9// ft
Acetone Sample Volumef
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
i
TARE WT
NET
DATE/TIME
9-i>/
o 6 K'
S-/^
BEAKER 1t
* -7
(,7:WW
& 7,^r<;7
67, 6V6/
^•7. 0 . WOO
5"t> . O(j<3C>
Sn ,,^r-r' /
5^7 ^
BAROMTRC
PRESSURE
•2 CA ^^
£<7- f/ g"
•Z9, 2 ^T
Initials
/^c^
/^r^
/^ r-/?
o
i
o
o
I
CT-
(BLANK GONG.) x
(ACETONE SAMPLE)
WT GAINED
(C) _'_-
,
TOTAL PART1GULATE CATCH (A+E+C) =.
jng.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT L
ES PROJECT ftO
RUN No.
Placed in Dessicator: Date/Time 9- 2? - "8 *? /
STOVE MODEL No.
POSTEST
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
o, _Zy
c» *}' V 5"
q - 2 5
/o Z ^
9-25
/ 5^-z>
9-/7
FRONT
FTLTF.R it
^^- 3
./vvy
* / w;>
. /v^s
a/^l^
, /ZoV
^5 .^^3^
BACK
FTF.TFR II
r/94~- y
c^2J^
* t Z /;,
*/?.l3-
® /'•?, /?.
« ;^./6
~ O.ooo^
CALIBRATION WT.
WT AMOUNT -
PRE WT
o V 9 9 <}
« /it>Z'
« ^fiOC>
POST WT
» 5<:» D /
«> V^f^)
0.^00 f
ROOM CONDITIONS
RELATIVE
HUMIDITY
5b(^^
-------
CLIENT
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page of—
RUN No. C
9-/S
BEAKER It
/?-r
7^,'3ZV/
7^, ^z3,r/
7/0, 3^V/
7^* 3"? W
7^ , 7. S 3 7
c> . o 3^y
CALIBRATION WT
WT AMOUNT =
PRE WT
£c>, oeoc>
Sc>, &oa&
C) f^ t CWO I
POST WT
V?«?W
50-*aoo /
$a ,t~L-
ROOM CONDITIONS
RELATIVE
HUMIDITY
S^^r,
^^ 7
tf6&7o
BAROMTRC
PRESSURE
?-94
z^.^C
Initials
/^•1C ^
&cf
/fafy^
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C).
TOTAL PARTICULATE CATCH (A+E-i-C)
', v
_mg,
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page I
RUN No. CC^-SG-//) Placed in Dessicator: Date/Time
Q.
ES PROJECT # P/23. STOVE MODEL No. ' W;
5V> . /'^o /
POST WT
^0 . ^^^ /
50 , ^rf^r)
ROOM CONDITIONS
RELATIVE
HUMIDITY
So Q>& S'.
VI o
S/9.S mg.
-------
CLIENT :
ES PROJECT
17-3
PARTICIPATE WEIGHTS SUMMARY Page / of /
RUN No. CcT^-5^ -//? Placed in Dessicator: Date/Time 9-7.7~
STOVE MODEL No. ^c -/ So
POSTEST
1 WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
^ - 7. <-/
o d P
^.7.6r
/.o //y
CALIBRATION WT.
WT AMOUNT =
PRE WT
> 6'^OC-
i D&P/-.I
POST WT
. V-x^y
« YW
ROOM CONDITIONS
RELATIVE
HUMIDITY
So&C*g
y&&6~?
BAROMTRC
PRESSURE
?^ C'Lf
Z1.9Z
Initials
(
/** c^
/t* c-/e
o
I
o
o
Ol
I
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
/ of /
CLIENT
ES PROJECT /R.O S2.3
RUN No. CC5-6'(?-)£ Placed in Dessicator: Date/Tirne_lllOl.
"STOVE MODEL No.r:^ / ^o ^
Acetone Lot It \(I ^S> ^-7/7
POSTEST Acetone Sample Volume «"
WT 1 .
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
(
TARE WT
NET
. DATE/TIME
' <7-2-V
&&V4
W,
^-1^-^
BEAKER It
A-^
b Z ,t 5 1 7
£S. ?^;/^
@£gr
V<^7
BAROMTRC
PRESSURE
29.94-
29,95?
Initials
///<-^
/7/c ^f
o
I
o
n
Ln
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
o . o
TOTAL PARTICULATE CATCH (A+B+C) =.
^ 3
jng.
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
/ of 1
CLIENT ^ P/9
ES PROJECT R D /'Z.3
RUN No. CX<£-S£'//?placed in Dessicator: Date /Time Q-ZZ-ft?
STOVE MODEL No. <^C~ *-/
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
cj--zv
of;v^
ci-2$
/ft UO
9 -•2.5'
/ 5/<:
9-/7
FRONT
FILTER tt
^- ^
hm^
M7Vo
D.^96^
BACK
FTf.TRR 11
#?-3
* £?6S
• bISk
.63*76
ttn^/
0.6/0$
CALIBRATION WT.
WT AMOUNT ~
PRE WT
o $V' -if-
„ ^&oO
i ^o-ZsV
POST WT
- V99S
»yciLi<]
. W
ROOM CONDIT.IOHS
RELATIVE
HUMIDITY
^d^^s-
4^6 ^^ 7
^- &£ J
BAROMTRC
PRESSURE
7-C)?fr
•2 9, 9^
•2,9. 8 '$
Initials
(
^'c/f
MC£
/>!Cg
o
o
o
Ol
I
t—*
I
I—'
t-0
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
•' Run i ' CCL'5 - f
ES Project t %D /I 1
Wood Heater Model
Operators
!5O
TEST RUN INFORMATION
Attempted Burn Rate fKg/nrs)
Achieved Burn Rate (Kg/hr) 1
Primary Air Setting
Secondary Air Setting
Thermostat Setting
Other Settings
51"]
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (I)
Room Velocity (ft/min)
Scale Audit
Surface-Temp. Ave. (°F)
Cold Draft
Firebox Volume (ft-)
Fuel Charge Range Wt.
Pretest
Post Test
VC
TEST FUEL DATA
Actual Fuel Charge Wt.
Coal Bed Range Wt. 2aQ to ? ^
Actual Coal Bed Wt. 'Z.
« V ^ Fuel H20% Dry Z.| ,5^ Wet ll .
Fuel : Dry Kg \\ 7.
LOADING/TEST START OPERATIONS
By-pass £lt&ay (g 6>-j^^ Air Settings.
Door c^\CiJ '. HJ -^ Comments
Velocity Traverse ^
Temp
A 1
2
3
4
B 1
2
3
Ave.
Pitot Leak Check _
Static ^ ; 03 V
qfc
G-CC5-1-13
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AMD FUIM CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client ^P/V-\)pr Run
,
CC-S ~ I
Date £\-~Z.\
ES Project # j? Q
Wood Heater Model
Operators
Test Fuel Charge (o < o
Coal Oed "2.
Page
a
i
n
o
Ul
I
Time
Sampl 1 ng/
Clock
-LL,
Test
:uel
U.
(Ibs)
3,7.
I, R
2. A
±
Fl.ue
Draft
(In
Comments
. \;V -
. z.
1>< i
8.2.
^,7.*-
_" v iraH""-!
~-J*<**f.crr <*(-
Coinbustor Temp.
fa 37
&n
6 $<;
lo
fob/
9V3
Top Hear Bottom Right Left
Surface Temp.
Vfo? .
i//-/
Vol.
-?71
IW
322.
•377
^77
Stack
Temp.
?/
on .
Tun.
Temp .
99
37
Room.
Temp,
-------
ENGINEERING-SCIENCE, INC.
Client £/)/) Run
Date
I > gq
ES Project f
WOOD IIEATEU CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTIOH DATA SHEET
Test Fuel Charge /&,
Coal Bed
Wood Heater Model
Operators
. Page ~Z- of
'?.'
P>
CD
I
n
o
Time
Sampling/
Clock
H
v
> '7
Test
Fuel
Ht.
(Ibs)
T./0
0,7
I,S
Fl.ue
Draft
(In
M?0)
403 -K
JtO^
Comments
Combust or Temp.
55 -7/7
757
-72 /
?a
5/n
33-
/
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AMD FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £^/? , Run I
CC, ^ - /
---- ' '
Date
- ft
Wood Heater Model
ES Project. I RD /23 Operators A
Test Fuel Charge
Coal Ded -2-
, O
-/&, S Page"^3 of
B//
o
n
o
i
»—
i
I—*
a**
Time
Sampl 1 ng/
Clock
n
9,
2
10
•7 o "?-
•7 o
•l~l o
Test
Fuel
Ht.
(Ibs)
,0
7,4
-1
2T
Us-
0 ,
Fl.ue
Draft
In
Comments
Ct<,h&/o, C
Combustor Temp.
SS'/
59
A
//'i'L.
9
773
-7
lop
5-2;
Hear
Surface Temp.
SfZ.
iVZ
^2_
Dottom
37 /
35
Hi glit
Left
y§r
f£2£
4/6-7
JL
3VZ.
i^3_
j^
'-X V
Stack
Temp.
"3V?
V7/
Oil .
Tun.
Temp.
/aZ.
53.
5-3L
•95"
-7 V
Room.
Temp,
87
7
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £ Pfl Run
CCS-
Date
ES Project, j
Wood Heater Model
Operators _ft*c A.
3 1
.03%
•'
••
Comments
'
*
Combustor Temp.
V/
Top
/of
Hear
Surface Temp.
Bottom
RfghT
TeTt
Stack
Temp .
Dil.
Tun.
Temp .
Room.
Temp.
-------
CCS-56--
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC \5<2>-S
Date
Samf
; cj ^ 7,^ ^ £j«
>li ng Location a)"*) — |
Sample Type
Run
Number
Start Time
Stop Time
Probe Length and
Type /i" *rt»-%»
V\f,^r- Pi tot Tube Coefficient ,9.^ u
X-. p £-
01
i
* — '
i
i — •
OO
Clock Time
Sampling (24-hr
time.min Clock)
O I ~2-l.<>
ID -fTi.-?.^
~'i .'' •' ?- 7. V'C"
( • X *•)- )
<•'< 0 .' ?..'•%
1 fr 1 "z, 7 <
<&O f -?,3<
q & fbYT
[frO l^^
\ln Itfo*?
110 fH IS
IV) m~i~c> \^ iC.
^^ / ^ 'Z ^
~ioc, t<5<-;/
-*? / ~~) 1*5 •5""2_
\ t2, ^^P /J^ — S —
Gas Meter
Readi ng
(V ) ft
"~7 *>/.&£* "Z-
-><:,:-, /
7<' A ^-/
~V' v « ''
'-I'-^L, <^>
•777. ^
76>7* ^
79%, /
7^f5» V
^^)3^ *9
5^^9* ^9
C7 1 {/ "7
^2,
C ^ J iJ
n/ / *
ftTA 1
^ ,O*3)^?
n , < i "'/-
»;•.' ~4(.
« O-XA
» <^» 3 £•
t O "*,(,,
« /? T3"<£
J £^l *3 ^»
x> ^0 ^> ^/
• * ^
' £) "^/S
„ f) ~2)fy
*0 ~3C?
" o "7^-
• o ^4
• e> '*>/?
. 0 "3 C-
. 0 1b
-^ c/ X/
» o ^ <&>
Orifice Pressure
Di f ferential
( H). in. H?0
Desired
«- ^3
- fjj <^s-i
Actual
^<~^
,. >.V s
j- '•'/-,
-9S
^ ^^
„ <7 c
' 7_^
o <9 ^
« <9 "5"
ocl^
" ^^
' y ^
(O ct £?
ci ^
e 9C
« <^ £7
» Q G
' £->
- <7 ^
Minutes
TEMPERATURES
Di lutltTn
TunnXl
^U
10\
^'A
qi.
Meter
In
$7
^i i,
s '•'-•
C^ 7_^
-,-> "?.
9 5
9^
97
^ft
*?9
9 »
9 ff
97
9 "9
9 o
<5<9
9 9
9^
9 S
^7
^ ~7
9 >
Meter
Out
£V2-
,^ 7
<• . .
S' <'--
tr1?
¥, *%
°)o
9/
^ "£•
q T,
<9 3
<9 3
^^
9V
9.'^
9* ^
94/
S5
vjy
^'?
*7 ^
-=? ?
Filter
S 2-
•
Impinger
/ ^ •
c M -/f,
>; :. .~7-.-r'
&"? 7 ^
*?d> ^"^
/ cJ C& £f~
^y ^^ O^ *J
rt Ci y^ -^
^^ /^^
89
^ "2,
Is- 3
•& *? ^3
^59 ^ 3
S S" ^3
^ ^ <^> V
89 if ^/
&R.
S If
& y
(^ *-/
/) 7 /• V
«?
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater_
Date CJ--
C.C - /
Sampling Location /-
Sample Type_
Run Number
Operator yp\
Sampling
time, min
lock Time
24-hr
ock)
Gas Meter
Reading
(VJ ft3
, ST
Velocity
Head
(&PS) in.
H?0
Orifice Pressure
Differential
(AH).-in. H?0
Desired I Actual
TEMPERATURES
Dilution
Tunnel
Meter
In
Meter
Out
9 ?
Filter
Impinger
Pump
Vacuum
in. Hg
•2 -
Flue Draft
in. H20
t, 7
> o
3
Z , o
-2
o
9?
9V
2-?<3
323*.
%?/•
93
9T~
£.
^L.
ttt><=,
zo
95
99
2X^_
93
"1,0
0 Tib
93_
3^.
_.._2£
0
C?
97
92-
^2_
tf 0
92.
/»^> -:?
5LL
^Z.
0
"Z- /<
73*
95
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater (C.C--
Date 9 - Z y -
Sampling Location_
Sample Type 2
Run Number C C
0
22.
.0
_.£2Z
"7
3
^
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
o
i
n
n
I
NJ
Wood Heater CC^ISCs-^i
Date 9-7.4-©0/
Sampling Location \ST- \
Sample Type \
Run
A56r-
Number CC£S-"Sfer— I ~K
Start Time
Stop Time
Probe Length and Type . y i," •p/«~s>ii»
Pitot Tube Coefficient ,q^ ^
Assumed Moisture V
Operator \AiV\v-V ^ .^rVV^ ~
Ambient Temperature -'_, .-
Barometric Pressure -2 ••/,-.,ftf/D
Sample Box Number ~2>
Meter Box
Meter H
Number "2>
Pretest Leak Rate tCCfj c^_ /S;/
Post Test
Read and Record All Data Every IO
Clock Time
Sampling (24-hr
time.min Clock)
D I "^-Ifs
//,> /2--2<
? n i ?. ? -,
W' / -7 JT, ?*?
/V^5 6"
)1O /Y/*7
/'V) yy 2 ^
/^<9 /V'Vr
/ 6 (7 - mn £>
/ 6>o /V 5"<"
\~JO 1 3o*>
\ ?*>o IS '-5
/ "? ^> /$" Z. •T
•^Z.^2? / S 3 5~
*~l_o(f> \ 5y/
2 //? /5V^
•2/9 / ^-S"-^
azb /^-pS
Gas Meter
Readi ng
(Vm) ^
1^3,261
-) V $ «',' .
"/ 9 -'. v "'-,
7 S X . V
-7^^ ^._
-7 73*. S'
991?. 7
7&y , I
Iff! . "2,
•79V. <5
7f9, 7
j^ ^ O
^ / ^) f ^7
f12.<^)-' /
^?<* 9
H.J6, "7
•gy/f 5
.ft *-/ /
|P V~2) A^V*
^5-7 ^
A ^^^/
"65? "7*
Velocity
Head
( Ps),1n.
H?0
d), ^'.^Qi
i^rii "//,
"? ,'i "' / •
0 .': '2 /,•-
d <'> "<,-•-
/> <9 3A
fo"2>^>
fs»'T>£
oO ^/j
0 S*) / if
• p O ^/9
Of) ~~l (f>
• , f}^l,
, 0 ^ {/
*f> -z,/,
*£> '3fc
A r>"?>{t
*c>73G
00l£
V< or
jL)f.iO C»
Orifice Pressure
Di f ferential
( H), in. H?0
Desi red
i 95
f f* :'j
•
O.n
/ k
Actual
< ••"/' '--'
* L'/ -''
,9 ^
"9 s*
^ ^*
<& 5
fCf^
tCf ¥>
°l 7
9<^
7<^
Meter
Out
S ?
' . •
,s ^>
>' ' >
,s .\
87
c)<9
Cjf/
9^
g 3
93
9V
9V
95
9 5"
Tfi
£jy
9Y
^//
93
Filter Impinger
£^c!_
,f '' •'-•.•;-
'-; ^- ''•/
°J £> <$> ^~
9^ /*/
Qn 6-G>
Ztf fol
^9 ^ /
S1^ <^/
"&9 ^ 2
^ 9 <^ "Z.
59 /i 7L
5? <^7 J
87 ^-3
/^ y' ^ 3
25 Sr ^ ?
^ T_
t^^. ^3
S S <> S
Pump
Vacuum
in. Hg
"^— _
?
'/
•7
->^
•?
2-
2-
•^~
-^2__
•o_
"Z_
•^
"2^
2>_
2
~?
"2_
•7
Z
7
T-*
Flue Draft
in. H20
n
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater C CT — / So
Date
o\ ^ ~~) ) OL Q
/ * — / i' i
l^e 2^3
Sampling Location ^ S Ll^-o^/ J^Z^f 4<^^> "~~^
Sample Type "2.
BX*T"£-
r\
Run Number c C £> - S'<^r - //S ^-1— '
Operator ,////• /^ 4J //
i
n
n
^\ Cl ock Time
S amp 1ing\{2 4-hr
time, min^^lock)
27277~ " — — ^-£5$.
2.3,^ • y£,i^
2 V^> //£/§•
"2- ^»o y/, ? **
•^ 7/9 / > (/i^
2-. ^r; /^> ^5"
-]^Cf(y )^O^>
_%££> /~7;^^
•3~%
3y/9 /74"<^"
-2, <^o yg<7 ^"
" ( L1 1' /Xj* / J
-? 76-1 yfs2C
"?7 "$ y'S'^^r'
•^o/xj / 55 -^5^
39/7 /crf>L/c:>
^/tfb 1 7i*y*\
u)O /^o^
, 7
2S9S-. 9
<"/c?V * /
^9/.>4 e ¥
A ;// *^
*.f5'
<7 ^-^ 7
"? C> "5 ^'
d» <2* ^^
« o "-?<^
.(3'^>C,
• o 3fe
- "? ^
^ o B<^
« r> "3£
^ c> ^x.
^G
.*&*>/(,
t> & ~?>/->
^ f P~,
/, ^ 3^
- a ^6>
» o 3(/
/» rl ^?
Orifice Pressure
Di f ferenti al
(AH), -in
Desired
"i I^Le-
HpO
Actual
f 9 5"
/ v ^
* ^ "S"
-* 9_S
*-/ ^"
-9 '
o "9 ^
v
%6>
8£
37
c3
/oCJ
/, 5L
<<, •?>
Pump
Vacuum
in. Hg
"2L x>
Z ^ (T-^
7 0
2 , ^
'2 „£>
?-Q
2-0
"Z .- o
7 . c>
~~L 'O
2,0
T- /6J
1 '
2,x
-------
o
I
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Ln
I
1—•
I
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U)
&=Ea BsiS
3^rvi ^^nrVJ'
o/
ENGINEERING-SCIENCE, INC.
nri_iMu ut\ i n ^i,uiii..y '
Wood Heater- C C - / 5"£>
Date
9 - "z- / - 8 9
"P
Sampling Location C$ teJ^&c/ z£/Qzs* 4<^-£? , O
Sample Type •?. <
^/*TG-
Run Number CC ^? ^x'
Sampli
time
\ Clock Time
ng\(24-hr
min ^vQlock)
"174775— — — . — /_23£
^ 5"o /^/V?'
L/ &o i 9 *-!*->
HI o ~2,*>
V ?5<2 'Z-5>/c>
V 7(0 "^02?
5^0 2 ~2.^S
5 3<2 "2/y 9
_j5"^£> 2, ^ /$"
55c? "2-/'25*
$&<
~'-Jy<
0 "2./3£~
D ^ / /7«< 7
; ^O f n
/A^7
Vel oci ty
Head
(APS) in.
H?0
,,
* & ~L,fo
*
(> f9 3£-
c <") 3 V'
*r>"?^
^ ^ ^ t7
._, ^ -3 A
' & ~3)^-
Orifice F
Different
(AH), -in.
Desired
ressure
.ial
H^O
Actual
'> 9 ^
> 9^"
< 9T
„ y-j"
., 9s'
' 9$
f^^)
o 9 <*
^9"5"
,9 ?5
- 9 ^"
' *? 5"
TEMPERATURES
Di lution
Tunnel
Meter
In
9y
9y
Ox/
O 'X
91 3
9 y
<^r 3
i^?1 ^3
9 3
<9 -3
93
q~$
Q"Ls
9 Z.
'\
9*2i.
-
Meter
Out
7/
9/
9/
"7O
tf 0
7/
9<^
7^j
<7^f
i/
?.*L.
Filter
^5-
S 5*
K 8"
s ,*V
.517
87
g 7
S"^
•J? ^'
^•5"
89
g" V1
c^
Impinger
/£ 7
dr. 7
^ 5>-
>
^ o
^)O
/-, 0
•
Pump
Vacuum
in. Hg
"?.. s. c5
? rO
7 ,• cv
? x (--,
•Z . o
Z , o
~? *<*>
2 cTj.
2 «,2>
1- - C?
?»o
~2'O
~2_ ,c>
-?,O
Flue Draft
in. H?0
-------
FUEL MEASUREMENTS
Date _ 9 _7,/ — ^c/ Wood Heater Manufacturer
Project No. ' ~ Wood" Heater Model
Run No.
Circle One: (pretest jjjeK ^-- Test Fuel
Fuel Type and Amount ?xT \/ 4x4 1x4
Ideal Load Weight _ ' _ Actual Load Weight
Fuel Piece Length _ 1 _ .
Moisture Meter Calibration 12% _ / 7^ Q 22% ^-2. o
VJvv T*~-,_ °F "7 ' • .
2
3
4
5
6
7
8
9
10
11
12
13
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)-
Piece No. Readings Average
Overall Fuel Moisture Average .
G-CC5-1-24
-------
FUEL MEASUREMENTS
ttfc*
Date
2-1-8*7
Project No.
Run No.
Wood Heater Manufacturer
Wood" Heater Model
-------
TEST
CC5-2
M23.4Q
51A.APP
-------
, Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
1st date: 9-25-89
Run no : CC5-56-2H
1st time
(min): 490.00
Chrg ut
(Ib uet): 40.90
run
time
(min)
0
60
120
180
240
300
360
420
480
490
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
036
036
036
036
036
036
036
036
036
036
Units l=metric,
2-English:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.7. uet):
Burn
stack
temp
(C,F)
92
109
97
107
97
108
97
110
96
96
DGM
rdg
(m3,
58.
88.
119.
151.
182.
213.
244.
275.
305.
311.
ft3)
008
700
700
000
300
300
300
000
800
073
DGM
temp
(C,F)
71
77
80
80
81
80
79
' 80
81
81
Samp vol
2 (sm3,scf)
0.995 246.612
0.99
28.56 Flou rate
29.84 (dsmSm.dscfn)
0.1963 138.23
18.01
rate (dry kg/hr): 1.86
DGM dH
(mm H20)
(in.H20)
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
0.950
vel
(ffl/min)
(ft/min)
775.43
787.28
778.94
785.90
778.94
786.59
778.94
787.97
778.24
778.24
PR
(50
102.7
98.9
102.2
99.5
101.2
98.5
100.9
97.5
101.2
dDGM
vol std
(m3,ft3)
30.334
30.296
30.420
30.420
30.072
30. 128
29.892
29.934
5.115
85.49
17.640
460.00
1850.00
vs/VraTs
0.01
vs ave stack
ave temp
(C,F)
781.65 100.90
o
i
o
n
Ul
I
fO
I
-------
tMethod 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
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
490
ORVILLE
CC150
ES
9-25-89
CC5-5G-2B
490.00
40.90
vel dp
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
036
036
036
036
036
036
036
036
036
036
Units l^metric,
2=English:
Y, DGM:
Pitot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.?. uet):
Burn
stack
temp
(C,F)
92
109
97
107
97
108
97
110
96
96
DGM
rdg
(m3,ft3)
58.001
88.700
119.700
151.000
182.300
213.300
244.300
275.000
305.800
311.035
DGM
temp
(C.F)
71
• 78
80
79
81
80
79
80
81
81
Samp vol
2 (sm3,scf)
1.009 250.127
0.99
28.56 Flou rate
29.84 (dsm3m,dscfm)
0.1963 138.23
18.01
rate (dry kg/hr): 1.86
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
775.43
787.28
778.94
785.90
778.94
786.59
778.94
787.97
778.24
778.24
PR
GO
102.8
98.7
102.2
99.7
101.2
98.5
101.0
97.5
100.5
dDGM
vol std
(m3,ft3)
30.778
30.675
30.857
30.914
30.505
30.561
30.322
30.364
5.151
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs
781
ave stack
ave temp
(C,F)
,65 100.90
o
i
n
o
Ul
i
ro
I
NJ
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD,.
DATE DEPLOYED <5 - 2 5"- J?5
DATE RETRIEVED O.£l£ (IN HG)
C,fTtr ^rrTi/v* F /a **>
TANK "2,9,9?' (--IN HG)
TORR ABSOLUTE "2. , 6~S^
WEIGHT GAINS
PROBE /•
WOOD CONSUMED (LB) V^
SAMPLE FLOW RATE PRETEST
KUlHAtihX Ctf 0 -(.LlL aliN;
POSTTEST
ROTAMETER £ ? =(ML MIN)
-l*(e
r.c /
(KG) /o.S5
PRETEST LEAK CHECK
START S. */
H20) FINALS. / (IN H20) LEAK RATE £ , "*, (IN H20 MIN)
POSTTEST LEAK CHECK
START V. % (IN H20) FINAL f.
(IN H2) LEAK RATE 0, 1_ (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN
COMMENTS : $ A/U ts) S
C02(%)_
C0(%)_
02 (X)
r, / 7
GRAMS MASS ArTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
t-^7_MIN.
MIN. + JO. MIN.!
DELTA
PROBEH-FITTING3y.Vfr£ V
SAMPLE LINE
CONNECTOR
G-CC5-2-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
'- Z5' 6 °\ PROBE
LINE _^_
COMPENSATE
TEST LOCATION £/? VJoerlcjTnd? JA L FILTER* 1
DATE DEPLOYED
DATE RETRIEVED 9 ~ "2Y» - *%
O, /
RUN//
TEST TIME
(MIN.)
STOVE ID CC
SAMPLER
FILTER#2 —
(HG BAROMETER UNCORRECTED)
PRETEST B.P To.gf,, (IN HG) _^
TANK 2.9.9^ ("IN HG) TEMP. 2/.Q (C)
TOTAL (MG) / 3/6
WOOD SPECIES f)oue Id <, F ,
WOOD MOISTURE (% DRY) Zl^b
WOOD MOISTURE
WET)
WOOD CONSUMED (LB) V
(KG)/u5S
TORR ABSOLUTE
POSTTEST B.P. "79,7 5
HG)
TANK
("IN HG) TEMP.
(C)
SAMPLE FLOW RATE PRETEST
ROTflXETER_£J£__= (ML MIN)
POSTTEST
ROTAMETER 61- =(HL MIN)
TORR ABSOLUTE 3 O g . 6
PRETEST LEAK CHECK
START ^ g (IN H30) FINAL C. "*> (IN H20) LEAK RATE ~ Q ,1, (IN H20 MIN)
POSTTEST LEAK CHECK
START?. 5" (IN H20) FINAL7 ? (IN H2) LEAK RATE &. 2. (IN H20 MIN)
POSTTEST GAS ANALYSIS
C02(%)_
C0(%)
RUN COMMENTS :
0 jj
"
^ £ • //
'-/"Z-
,- /V
02(%)
//
GRAMS MASS AFTER: FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST- +29. MIN.
PROBE-i-FITTIMG "3> VC 3-g ^ '
SAMPLE LINE "V7,
//3 CONNECTOR
MIN.
MIN.
T
3V. 3593
•7
0. 6J>6_L
-O ,6C0
G-CC5-2-4
-------
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
•
RUN No.£'<^' /'/QT-7/3 Placed in Dessicator: Date/Time_9_lJL
q~/ /3/O
STOVE MODEL Ho. CC J
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
cl-17
//.<*?
<7 -Z7
^Z^SS
*y - n
noo
q . / 7 - S *?
FRONT
FTr.TRR It
5^-1
-/^73
. /Z-73-
- /Z.73
-/Z73'
* /7./-Z-
O-Crote f
BACK
FTr.TRR il
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«/ 2.^^
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*/z^V
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,/2oS
-^.(900^
CALIBRATION WT.
WT AMOUNT -
PRE WT
• ^csa /
i 5" &-&o
« $oo£>
POST WT
„ 5~£>t>Cr
•Wr^
.V9W
ROOM CONDITIONS
RELATIVE
HUMIDITY
*iQt^lCxf
>^7«=X
o
I
n
o
un
I
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I
(A)
(B)
-------
CLIEHT
ES PROJECT KQ-/2'2)
PARTICULATE WEIGHTS SUMMARY Page of
RUN No.£X^'-^/)/'-2/9 Placed in Dessicator: Date/Time5zZZ
STOVE MODEL No. CC / ^
Acetone Lot U 9// *% -T.%
POGTEST Acetone Sample Volume.
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
t-
TARE NT
NET
DATE /TIME
1-Z?
/<.-? o
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6>%. 3^7^
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CALIBRATION WT
WT AMOUNT -
PRE WT
£> £> . <5£>0/
*:>&,£>&&/
$£> . 0O0&
POST WT
V9-999^
So, 000 <3
yr/, 99??
ROOM CONDITIONS
RELATIVE
HUMIDITY
Vz(P^9
-------
CLIENT
EPA
ES PROJECT ^ P n 3
PARTICIPATE WEIGHTS SUMMARY Page .of
RUN No.^T-^/lr- 1ft 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
^-7-7
/^<&
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. $000
»t/
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT
RUN
/-)/./- Zff Placed in Dessicator: Date/Tiine^I2Ll£f
ES PROJECT fl/7
STOVE MODEL No.
POSTEST
Acetone Lot \\
—
Acetone Sample Volume_3Z_2e2A/
WT 1 '
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
t
TARE WT
NET
DATE /TIME
^-27
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9-/9
BKAKER II
^- x^
£7, 32 2^
47. T.^7^
£7- 32, So
47 3Z^o
<^7, 3/ 96
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CALIBRATION WT
WT AMOUNT -
PRE WT
5& . ooo/
^0,000 I
^& . fro 00
POST WT
V9-9999
5o« oa o&
w.m
ROOM CONDITIONS
RELATIVE
HUMIDITY
V2 64^ '
V2<®7/
V^^Jo
BAROMTRC
PRESSURE
^>, X/
3^/^
3o . / 9
Initials
MC£
JhC>#
\
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(BLANK CONG.) x
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WT GAINED = , •-<:••
* QQ *%• V (C) —
TOTAL PARTICULATE CATCH (A-i-B-i-C) = ! -~>" ^
-------
CLIENT
EPfl
ES PROJECT T) /2 3
PARTICIPATE WEIGHTS SUMMARY Page, of.
RUN No.£c'5"- ^^ ~ 2/) Placed in Dessicator: Date/Time.
STOVE MODEL No. CC - /'yV
POSTEST
Acetone Lot U *7//^ .
Acetone Sample Volume <£>
WT 1
WT 2 ..
WT 3
WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
9-27- S1?
U 1^
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9- ?o- 89
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<^7^9S/
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& 7,08^7
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CALIBRATION WT
WT AMOUNT =
PRE WT
5^.^trt5/
S<* }
5& . 0000
POST WT
H9.W}
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V9,W7
ROOM CONDITIONS
RELATIVE
HUMIDITY
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT £_
RUN
in Dessicator: Date /Time
ES PROJECT /?P ) '2 3>
STOVE MODEL No. r? ^ - / 5
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
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DATE /TIME,
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• ^ooo
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-------
CLIENT jC
ES PROJECT RP
PARTICULATE WEIGHTS SUMMARY Page of
RUN No.cy^-5'(r 2/S Placed in Dessicator: Date/Tirnef2liL
STOVE MODEL No. CC -
POSTEST
Acetone Lot It °l 11 *3
Acetone Sample Volume
WT 1
WT 2
WT 3
HT 4 .
WT 5
FINAL WT
i
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NET
DATE/TIME
0<3
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TOTAL PARTICULATE CATCH (A+B+C) = "2. Z 6./
-------
CLIENT ±
ES PROJECT /3 D
PARTICULATE WEIGHTS SUMMARY Page of
«
RUN No. CC.*>'-^&-Z% Placed in Dessicator: Date/Time9'?<£'%*?
STOVE MODEL No. C~C - J
POSTEST
WT I
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
9-Z?
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8
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S** CJO
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I
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I
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
Run * '
ES Project t R Q 11 3
"Wood Heater Model
Operators
TEST RUN INFORMATION
Attempted Burn Rate I/ Fuel H20% Dry 7,1/tk Wet IS-
^~ ^ Fuel: Dry Kg f 5' , ~L\ \
LOADING/TEST START OPERATIONS
By-pass Clo^-^ Air Settings
Door o{U/y
Velocity Traverse
p Temp
A 1 0.63^ I&&
3 £>voMl log
Comments
B i
2
3
(t>B
Ave.
Pitot Leak Check
Static
4 6.035
4 ^0*3 1
G-CC5-2-13
-------
ENGINEERING-SCIENCE, INC.
Client t^
Date
ES Project. 8
t/
WOOD IIEATEIl CEIITIIMCATION TEST
TEMPERATURE AND FUEL COHSUMPT10H DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators (j
Page
_/_ of .=1
en
i
o
o
i-n
I
to
I
line
ampl 1 ng/
lock
IC6Q
_L&_
llWQ
( 7,10
Test
uel
•/t.
Ibs)
5,0
7.6
M:
Fl.ue
Draft
(In
,077
^5W
°'Q7-?
Comments
S.O/7.CJ
iVVxr-
Coinbustor Temp.
line,.
/32-Y
I/ BO
ZLI
50,0
Surface Temp.
I'opl Rearl Bottom' [night I Left
37-3
y?8
AL5.
if, 3
IQ/
35 y
35^;
Tex
3 eo
3-rz
22^.
S-o /
SJo.
Z3
•aSG
5VY
Stack
Temp.
74 z.
2Y.
5-7V
Oil .
Tun.
Temp .
/oy
_T2.
/a y
Room.
Temp,
20_
2L
76
7/
76
7-2.
TV
7.
JZZ.
7V
-------
ENGINEERING-SCIENCE, INC.
Client FPA -O^ Run I
Date
ES Project, j fch
WOOD IIEATEH CEIITIRCATION TEST
TEMPEUATUIIE AND I:UEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ded
Wood Heater Model CX
Operators U^U(-\ ^
"7s* of 3
o
I
o
o
Ol
i
Time
Sampling/
Clock
/
/7.3Q
17,5.
/'?
IH1&
'fVZ O
Test
:uel
Wt.
(Ibs)
1,1
^
,3
-*>•-)
. -9
/.
jQJL
0,0
8,7
Fl.ue
Draft
(In
P.£^S
06-?)
ft5S7
Comments
r/*o / '2-"? /it/si/
5L1
Combustor Temp,
937
95"7
rf V 5
// "1
// 7 3
J7.7JL
o -7 ~*
/^7 ^
[op
5/7
7VY
^M.
Hear
Surface Temp
V5/
y
5VZ
V77
VO
Uottom
•33~7 •
39
'3 vy
uTgirr
5V7
5-30
573
5/7
So 3
^75
TeTt
rs1 ?
I2/_
^7-2.
5V. '5
V V.S'
VV
Stack
Temp .
x/y
•793
7/0
^37
6s//
Oil .
Tun.
Temp .
^2.
/a
79
75
/6V
Room.
Temp.
7V
71
"7"?
•73
7V
-------
ENGINEERING-SCIENCE, INC.
Client f:p/y-O$rr Run
Date
ES Project I
WOOD IIEATEIl CERTIFICATION TEST
TEMPERATURE AMD FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ded
Wood Heater Model <-C/^
Operators CQ./4K \ •
Page -^ of
3
i
o
o
Ul
I
Ni
I
Time
SampH ng/
Clock
/g/0
Test
-uel
Wt.
. is
7,9
2.-S-
Fl.ue
Draft
(in
Mi
/67^
Comments
i•^^^ 0,0^
Combustor Temp
3
?
/ z-/ %.
8
?^-
77
fop
Rear
Surface Temp.
V73
ZZL
Uottom
33S"
3-72
37 /
UfgnY
5V d
^- 3
Left
J^7_Z
Stack
Temp.
6,17
7
Oil ,
Tun.
Temp,
±2.
Room.
Temp.
73
7V_
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater C.C- - 5
Date 9- 7,5 - <5 T*'
Sample Type
Run
Start Time
Stop Time
Probe Length and
//••'P
Type . ,2." ,/«-.v^,
rA«Sfc- Pi tot Tube Coefficient ,97 "
Number Ccc, - f?6 — "Z-A-
Operator t/^vVvA ki^c^v.
Ambient Temperature -7 /
Barometric Pn
Static Pressur
Filter Number
Meter
assure "T. 1 , cf
7O /ZiO
&d l2,J>O
fO ) T,^ d
to® /z^O
1 10 /3c*>
ll& l3>tC>
l^o /?>io
/•vo y^-?o
/sv? /i*yc>
/6c? ;?>5O
/7O /^f>6
1 HO Ml*>
\ C(D (H ?-c-'
•loo /tyj0
•Z/6 {tjtjb
7/l£> fJSO
0 ^0 ^^fc
n-Vo / ^rt5
Gas Meter
Reading
ft
5 ft .00 8,
^^, a,
"73 1 *-/
7§P ^
(5^ A,
^i°'7>to
, C»
QOICc,
0\.6*3 O
0vC>"2>C
L\ C» *^ ^t>
C. O"1i
O c ej 5 /,
o » /:> '^ 6
i? • <; • ">> t
O « o "^ C' '
c^ ^ ^^
<^) , o '5 (^
a, 0^6
Ci o '3 C?
^>O^ 0-
rx>3c
Ori fice Pressure
Differential
( H), in. H?0
Desi red
,*i5>
-.^ S
.OS
,^S
"7'S
.'rS
,^3
- 9 ^1 S'
. 75
o 9^
f 9 9
, "7S
.7-5
Actual
AS
iVS
. *?*5
*?S'
V15
'*?*:?
i*7'S
7S
^/c.,
(<7£7)
-9S
* ^y ^T
- 9 *T
* c/ S'
•* C^S
o 9^T
o 9 9"
r ^ h
. 9 Y
^99
'9 5
i ^X
. *7 S
.75
TEMPERATURES
Di lut>on
Tunnel
Meter
In
""? T—
7S
"7fe
g*S
r?/
c?"^
gty
&<-/
R*N
/=>c;-
ss
$*?
"3^"
^ "v
1? ^
S S
S ^
ft 6
^y
77
•7 ^
•TV
79
So
So
9^(3
So
So
^o
80
^0
So
S ^
^ -'$"/
c^ / 6 Z.
c?<5 ,5"^
c?^' -S' ?,
Pump
Vacuum
in. Hg
•^
^_
2—
^_
^
•^
-£_
2.
2.
^
-^,
p
2L
2,
J^
^
2_
Zx
^
"Z,
7
p>
-2_
^
Flue^mt
in. H90
r> ytV^J C^/^
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater
Date <-)"
Sampling Location
Sample Type rl5a-
Run Number
Operator (^
-Z/\
A Hr V,<
Clock Time
Sampling\(24-hr
time, min^XClock)
i Sz.o
Gas Hater
Reading
( ft
Velocity
Head
(APs) in.
H?Q
Orifice Pressure
Di fferenti al
(AH),-in. H?0
Desired Actua
TEMPERATURES
Dilutxrn
Tururel
Meter
In
_3£_
Meter
Out
Filter Impinger
Pump
Vacuum
in. Hg
Z.
Flue/Draft
1n/H20
. 0
7 7
YS
,97
^L
7'?
. 03
V. C
JL^
23-
22.
370
, 3
i ; s"
&. o is
7-5
^L
/730
s
.9s
6_a
6, a 3 cf
s
V.c
C^.c-^Q:
o
I
n
n
l_n
i
N3
I
I—'
00
O.Q'^0--.
, 9.
7
1 70
,9S
So
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood lleater_
Date
Sampling Location
Sample Type
Run Number <
Operator yp
\. Clock Time
Sampling\(24-hr
time, min^v^lock)
~ — .
^e: f^»o
^oS^
"^1 I.6T3
7.$-3,o65
Velocity
Head
UPS) in.
H90
<^'.o 3 ii
• o~*>6>
Orifice Pressure
Differential
(AH).-in. H?0
Desired
.?S
Actual
r ^
.
-------
I* '^flaill Xl-iLl1_>'i
tH-Lu^ ^L-juifJ
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Woo-d Heater CC/5
Date £7- T,^ -f^
Sampling Location "j^-f-ii-/
Sample Type
Run
^Sfr-
Number ccs ^ c ~s_'T\
Operator I^VAVA. ( \ f-ViA.
Ambient Temperature 7/ "
Barometric Pressure ~2 9,
Start Time //• IU
Stop Time
Probe Lengtli and
Pi tot Tube Coeffi
Assumed Moisture
Sample Bo>
Meter Box
Meter H ,
Type /^" ^/c-s.^
cient .-f^ ^
-Y//
c Number
Number
44?
H/i* Trc ^ o
Pretest Leak Rate £>,£>o/ <£L /ti'f
Post Test Leak Rate <3,t>c>/ (^ 3 '/
Read and Record All Data Every <&
i
o
o
Ul
I
I
0
Clock Time
Sampling (24-hr
time.min Clock)
S /I J°
10 //zo
20 /1 30
30 \lHO
L-/O 11*50
«5'c5> / 2£>G>
6O /^£>
7B» /2-ao
C(0 /3-^C)
/oo /•? so
no t^j®
/££* r^/e>
/3o n-io
HfQ /"V^
/•so /-wo
ILO /^•>d
/BO tHt&
tfo lH~vc>
•l£>° £^/3O
i,lP l'-tti£>
?,?£> ,
Gas Meter
}eadi ng
S/^. col
61.0
"f3><^
*7&^
fi"5 Q>
^(?.r?
v3< g>
^j . c/
/oV- /
/6 ^. '2-
1 / */~ ^
//9 , "7
^y. «?
3o „ /
y-^5e J3
/Vo , 6
Ax ^r S?7
y 5y«. / „ 5~
/
o.c3c^
<^^ <^-
^03 (,1,
OiO'^^.
CtD3 Q>
0,o S;<^
tf'.'-'T ^
(Ji.^30
. CV <::• "^ , n 3 6
_D^ rt "5 6
O,)/j "? 6
"7 /"
0 , o 7? o
o 36
/j> . "^ 63
O ><-o o
95
<. ^S
cV>
<95
,75
,9^
« ^ ^
. q <;•
UQ 5"
^> 9 *7'
^9 S'
, 9 *?
,, v <•
*ci "S
. S1 ^
. <> ^
, c- "^>
Actual
.ri •=.
• 95
' r/S"
c ' *^
L^S
'^S
,9 "i>
i ?5'
/ ^ 3
. ^5'
, o 5
-* ^5"
- / ^
* 1 ^
i! ?S"
- '? 'S
? -s
Minutes
TEMPERATURES
Di lutton
Tunp^l
Meter
In
-7 2
•7~>
c5o
(§>/
^2,
<£?3
c5?'-^
&<-/
f^ ^,
•gy
" i n*S
Meter
Out
1 /
•7 2_
~7\
-7«=>-
76"
7^
-78
7'-?
7-7
77
?5 <^
79
S<5
S;<^
S<^J
KM
79
97
fro
^^
c5^G
c^ /
C_i /
Filter
Impinger
^ ^ ^^
7V T/
7S V^
75 V£
7? V^
^*s\ t-J ~~~j
^/ /yf (ill
<5o v
'7^ ^^
79 sy
7S7 ^"/
7? 57_
5<3 • 5" Z_
8V ^?
5
~>
jr
F»rt
^/^
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
-s -'25- ->g-v
Sampling Location
Sample Type
Run Nurnber_
Operator i
CCS -
Clock Time
Sampling\(24-hr
time, min\£lock)
Gas Mater
Reading
(Vm) ft3
Velocity
Head
(APS) in
H?0
fi.G'b
Ori fice Pressure
Oi fferential
(AH).-in. H?0
Desi red
Actual
.VS
TEMPERATURES
Di Iutl0n
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue/Bfaft
-tTK H0
s
L£l:
i7_
77
_2*i.
/ji
•^L
9-3
•7V
-L7_
JZ5_
7 '?
7?
372)
.o •> c;
V.
C1^, O '
7
1 cV
9S
- &
?>.*-/
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood lleater_
Date
-V .S
Sampling Location
Sample Type _
Run Number C'
Operator
(-\
\. Cl ock Time
Sampl i ng\(24-hr
time, min^^Clock)
' ~~~ — — — —
>iBo f-^co
^0 fc/2^
^
-------
FUEL MEASUREMENTS
f\cA:
Project No.
Run No. rv"
Circle One:
Fuel Type and Amoufv
Ideal Load Weight
Fuel Piece Length
Wood Heater Manufacturer D'A.
Woocf Heater Model
4x4
Test Fuel
1x4
Actual Load Weight
Moisture Meter Calibration 12%
vJ
-------
FUEL MEASUREMENTS
Date
'-l^z-?-,
Project No,
Run No. r
Wood Heater Manufacturer
Woocf Heater Model
-------
TEST
CC5-3
S\RDI23.40
W1381AAPP
-------
.Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
Tst date:
Run no :
Tst time
(rain):
Chrg ut
(Ib uet):
run
time
(min)
0
SO
120
180
240
300
360
120
180
504
ORVILLE
CC150
ES
9-25-89
CC5-5G-3R
504.00
31
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
.20
dp
H20)
H20)
038
038
038
038
038
038
038
038
038
038
Units l=metric,
2-English:
Y, D6M:
Pitot co:
Gas MU :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (2 uet):
stack
temp
(C,F)
91
98
97
92
104
94
92
102
95
94
OGM
rdg
(m3,ft3)
312.001
342.000
372.600
403. 100
434. 100
465.600
496.500
527.200
558.000
570.442
Burn
DGM
temp
(C,F)
73
82
85
83
83
84
85
86
87
87
2
0.995
0.99
28.56
29.67
0. 1963
17.57
Samp vol
(sm3,scf)
248.515
Flou rate
(dsm3m,dscfm)
142.25
rate (dry kg/hr):
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
798.24
803.29
802.57
798.96
807.60
800.41
798.96
806.16
801.13
800.41
1.39
PR
<2)
100.1
99.6
97.9
102.6
101.3
99.7
100.8
98.8
100.1
dDGM
vol std
(m3,ft3)
29.379
29.470
29.212
29.800
30.281
29.650
29.404
29.445
11.873
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
801.77
(C.F)
95.90
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
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
504
ORVILIE
CC150
ES
9-25-89
CC5-56-3B
504.00
31.20
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
038
038
038
038
038
038
038
038
038
038
Units ^metric,
2-English:
Y, DGM:
Pitot co:
Gas HU :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.'/. uet):
Burn
stack
temp
(C,F)
91
98
97
92
104
94
92
102
95
94
DGM
rdg
(m3,ft3)
312.002
342.000
372.600
403. 100
434. 100
465.600
496.500
527.200
558.000
570.436
DGM
temp
(C,F)
73
81
85
83
83
84
85
85
87
87
Samp vol
2 (sm3,scf)
1.009 252.115
0.99
28.56 Flou rate
29.67 (dsn3fli,dscfm)
0.1963 142.25
17.57
rate (dry kg/hr): L39
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
950
950
950
950
950
950
950
950
950
950
vel
(m/min)
(ft/min)
798.24
803.29
802.57
798.96
807.60
800.41
798.96
806. 16
801.13
800.41
PR
(.?.)
100.1
99.8
97.9
102.5
101.2
99.6
100.8
99.0
100.0
dOGM
vol std
(m3,ft3)
29.792
29.940
29.623
30.220
30.707
30.067
29.817
29.915
12.034
85.49
17.640
460.00
1850.00
vs/vmTs
0.01
vs ave
801.77
stack
ave temp
(C,F)
95.90
o
i
o
o
Ul
I
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED 9" "2- 6 - S
DATE RETRIEVED 9 -
TEST LOCATION/^?
SAMPLER SN# 9 «£ ^ Z T-.
WEIGHT GAINS
PROBE
LINE
CONDENSATE
FILTER*1
FILTER// 2 -
(HG BAROMETER UNCORRECTED)
PRETEST B.P29.7^ (IN HG)
TANK T. 9. £ o (—IN HG) TEMP. 7, ; (c)
TORR ABSOLUTE 3 -^
TOTAL (MG) 33.^
POSTTEST B . P .
. 1 1 (IN HG)
TANK
_(— IN HG) TEMP.
(C)
RUN,?CC-S°-
TEST TIME
STOVE ID
(MIN.)
WOOD SPECIES /^ot-e. />9S /v
RY
WOOD MOISTURE (Z DRY)
WOOD MOISTURE (% WET)
WOOD CONSUMED (LB) 31,'*- (KG)
SAMPLE FLOW RATE PRETEST
ROTMETERj£_21_= (ML MIN) <£_
POSTTEST
ROTAMETER
TORR ABSOLUTE Z. £ % > 5^
PRETEST LEAK CHECK
START ^,~) (IN H30) FINAL ^*. ^ (IN H20) LEAK RATE O . "L, (IN H20 MIN)
POSTTEST LEAK CHECK
START
V.I. (IN H20) FINALH,^- (IN H2) LEAK RATE O_
(IN H20 MIN)
POSTTEST GAS ANALYSIS
co2(%)
CO(Z)
RUN COMMENTS:
. //'
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
MIN.
MIN
DELTA
CC- *) PRQBE+FITTING "S%
CC->5 SAMPLE LINE
»oo_O
« o
CC - /? CONNECTOR 5 •
G-CC5-3-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED *? -2d>~ % *7
WEIGHT GAINS
"PROBE
LINE __-
CONDENSATE
TEST LOCATION £5 kJS L/) 5 FILTERS 1
DATE RETRIEVED
SAMPLER SN// 9 4> 2- 3 V _
(HG BAROMETER UNCORRECTED)
PRETEST B.PZ5-2_S_(IN HG)
TANK -LCj, &£> (—IN HG) TEMP. I/ (C)
FILTER//2 - 0.1
TOTAL (MG)
TORR ABSOLUTE
POSTTEST B.P.
TANK /<$ . O
3 4
(IN HG)
(—IN HG) TEMP.
(C)
TORR ABSOLUTE
E 3d*?./
PRETEST LEAK CHECK
RUN// COT-
- 3,5
TEST TIME 5>i10/
STOVE ID cc-x
(MIN.)
WOOD SPECIES
u e.
DR
WOOD MOISTURE (% DRY)_ 7. /.?
WOOD MOISTURE (% WET) /7,S "
WOOD CONSUMED (LB)^^-'
(KG)
SAMPLE FLOW RATE PRETEST
ROTSHETER ^ ^ = (ML
POSTTEST
ROTAMETER
(ML MIN)
START
(IN H30) FINAL2.lt (IN H20) LEAK RATE /,
POSTTEST LEAK CHECK
START V.6 (IN H20)
FINAL
(IN H20 MIN)
(IN H2) LEAK RATE Q > ( (IN H20 MIN)
CC
POSTTEST GAS ANALYSIS
C02(%)
RUN COMMENTS':
^y
02 (Z)
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
PROBE+FITTING
SAMPLE LINE
CONNECTOR
Y& MIN.
" MIN.
MIN.
MIN. DELTA
V.
•//
G-CC5-3-4
-------
/ of /.
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page__
0
RUN tta.C^G'-t/Pj'-Z/) Placed in Dessicator: Date/Time
STOVE MODEL No. £C-;"? (c>
c\ - ZV
//
4/z^>9
6.6/H I
BACK
FTF.TRR if
&9£-/y
• J~L/3
• f*-flL
• l\lt
*/Z//
. >~Ll~T~
~ 0,£>OO /
CALIBRATION WT.
WT AMOUNT =
PRE WT
•V79?
. ^e)OO
, $OOQ
POST WT
* $00~*-
. ° 7o .
BAROMTRC
PRESSURE
3o. //
3^/1 <"^
o
I
o
n
Ul
I
OJ
I
(A)
(B)
-------
CLIENT
ES PROJECT RDS2. 3
PARTICULATE WEIGHTS SUMMARY Page
RUN No. C ^^'l^ffi*^ Placed in Dessicator:
SiTOVE MODEL No.
POSTEST
_o£.
Acetone Lot it Q / f<3
Acetone Sample Volume J27
.£.
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
[
TARE WT
NET
DATE /TIME
3-17
, T-T. , 6~-t(C> /
£a , O&OA
POST WT
£o,oed*>
Ll9,Wlfj
ROOM CONDITIONS
RELATIVE
HUMIDITY
yz&?7y
Ye ©7o
BAROMTRC
PRESSURE
3^./^
•2>*.'*r
Initials
/fjC/t.
X^^yf
i
o
o
Ul
I
u>
1
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A-t-B+C) =.
- e.t'<-"<:-/
'"7f'^-L
Vi-^'
-------
CLIENT
ES PROJECT RO /2 3
PARTICIPATE WEIGHTS SUMMARY Page / of ^
RUN No.
9-??
&oo <*?
q-2¥
• ii ^^
9-/7- *9
FRONT
FILTER It
5>9/T- /5
• /Z%3
./3%o
'/$?? f~ /&
• >2*V
. /2-oZ^
• II&-L
, i -LO~T-
. J-LO<=\
-o.dool
CALIBRATION WT.
WT A MOO NT -
PRE WT
•V9J1
. $00 0
y $00 0
POST WT
i ^oo 2.
^9^
. V<7
•
ROOM CONDITIONS
RELATIVE
HUMIDITY
V2^9<^
v-?©^
^<^7/
BAROMTRC
PRESSURE
1°- //
^o./K
3*. /^
i*
-------
Page.
of.
CLIENT ,
ES PROJECT
PARTIGULATE WEIGHTS SUMMARY
RUH No. CCS-tJPJftA Placed in Dessicator: Date/Time. C/-?7
O"y/*>i^ c\ - 1~) &
STOVE MODEL No. CC - > ^°
Acetone Lot it 9/X ^
POSTEST Acetone Sample Volume.
5" 0
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
I
TARE WT
NET
DATE/TIME
q-1-)
•135-S
1- ?#
7 IW*
9- n~ 8°>
BEAKER It
/}-/<*
7^.7 4%^
7 6, 2WL.
Jo . Z VZL
7o .7.6 / &
• OZ6V
CALIBRATION WT
WT AMOUNT =
PRE WT
52>. &&o/
£>& , crtxyo
POST WT
5~O , O0<3 O
LJ9fv7&
BAROMTRC
PRESSURE
3tf./<*<
3o.n
Initials
Sli C^
M^
o
i
o
O
-------
CLIENT .
ES PROJECT
PARTICULATE WEIGHTS SUMMARY
RUN No.
Page,
of.
S*TOVE MODEL Nn.
POSTEST
Placed in Dessicator: Date/Time 9 ~
9 - 2 7 <§>
~ $
°
Acetone Lot ltj?//5L_
Acetone Sample Volume 9
WT 1
WT 2 .
WT 3
WT 4 '
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
^-27
J6 ^o
q~i?
T-^^r>
<>. '9
Initials
/KCf
\
/lfC.J
\
X>lC.^
o
I
n
n
i-n
I
(BLANK CONG. ) y.
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICULATE CATCH (A+B+C
-------
CLIENT
ES PROJECT ftO JZ3
^ARTICULATE WEIGHTS SUMMARY Page / of /_
RUN No.££"£"-56- • ?/9 Placed in Dessicator: Date/Time.
STOVE MODEL Ho.CC- /
POSTEST
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
9-?7
/ tyo
Q.--L7
•T-'bljfcV^
q -1%
//&S
9 - /7-%c)
FRONT
FILTER U
fl£~ '?
/.eS$-*sy$
• ^752,
.37^3
BACK
FILTER It
A£~ '?
.&9yv
j#
^^Y>
'^93f
^'9>. / •&-
3o./^
Initials
/H£^
A, ex;
/»<^
o
I
o
n
i-n
U)
I
(A)
(B)
-------
CLIENT .
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page of
RUN No. V5/0
6>9, Via
» Gfj^ 7
CALIBRATION WT
WT AMOUNT =
PR IS WT
$o.cc»f
So,0o*/
$A.00£>t>
POST WT
$0.00C/
$0.t~00
Vf.9^9
ROOM CONDITIONS
RELATIVE
HUMIDITY
y2^?.
^z©>7/
/Y\
(/ (Ad *5
BAROMTRC
PRESSURE
3o. /s
I*./ V
3*./9
Initials
s*c#
\
Sh£/{
-3. »oo99
*^e*c> ^ar,^
.00^^ (^ '°
( A-I-PM-TM - t-/n ^ . (a
U^> <~
/35
mi'
-------
CLIENT .
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page / <& t
»
Placed in Dessicator: Date/Time f."_
RUN No.
STOVE MODEL No.C«C>
POSTEST
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
^-L
• 3SS7L:
BACK
FILTER it
ft£-/(p
.6935
ȣf 32,
.^93o
*^,93o
, aGa
. $oa /
POST WT
.5**oT_
tSm
. ^"«^<3
ROOM CONDITIONS
RELATIVE
HUMIDITY
^®&1
^Z@7/
^^7^,
BAROMTRC
PRESSURE
3^- ^
3o./^
3<5./9
Initials
\
XH<=^
\
/«»C<
/^C/f
o
i
o
o
i
i
»—*
hO
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
•• Run f Q.C5 -
ES Project }
"Wood Heater Model
Operators LA-
TEST RUN INFORMATION
Attempted Burn Rate
Secondary Air Setting {Js fi> /\f/a /
Achieved Burn Rate (Kg/hr) l-.58g] Thermostat Setting
Primary Air Setting _ 5& ^"N. Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (%}
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
10'
W-C//0.0
. 7.
a.
Post Test
TEST FUEL DATA
Firebox Volume (ft-)
Fuel Charge Range Wt.
Actual Fuel Charge Wt.
i J C.
Coal Bed Range Wt. Z> ( to
Actual Coal Bed Wt. z. C.
Fuel H20% Dry ZI.'S'L Wet
Fuel : Dry Kg U, G^
Velocity Traverse
p Temp
A 1 A032.
2 0,037
LOADING/TEST START OPERATIONS
By-pass di&%G.cll Mr Settings
Door ^c>j~ ^ ^.^ Comments
A
Ave.
Pitot Leak Check
Static
G-CC5-3-13
-------
WOOD HEATER CEIITIFICATION TEST
TEMPERATUUE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client SfiA - VJft'E .
CC5-
Test Fuel Charge
Page
of
Date
ES Project g
Wood Heater Model CC (5c> Coal Bed
Operators \\\vAl\ i
o
I
o
i
i—'
•p-
Time
SampH ng/
Clock
0
/O (
/QSO
1 ( Z-0
Test
:uel
Ht.
(Ibs)
, Z,
0.0-70
16.S
R.S.
Fl.ue
Draft
(In
\?0)
,660
Comments
V Prx--.li>
CetJ h*<,
Combustor Temp.
7Z1-
J07-
111-1
77^
(i-7-7
Top[ Hearf Bottom riirgTvT[TeTt
/as
57V
Surface Temp.
ILL
"7)55
35-7
,V/7
32-3
357
350
3C7
><]Q
•330
3 •/
10$
Stack
Temp .
7&7
^S_
D11 .
Tun .
Temp .
/OG
^L
?V
89
/vio
/OX
Room.
Temp.
2L
12~
Z5L
2ttL
'X
77
7?
-------
WOOD IIEATEIl CERTIFICATION TEST
TEMPEUATUKE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client EPA -VJPC. . Run I
Date
ES Project, f
C£/5 - 56- -3
Wood Heater Model <32 PjTO
Operators U M- , Jj
Test Fuel Charge
Coal Oed
- Page £ of 3
o
i
o
o
*_n
I
OJ
I
Time
Sampling/
Clock
17^50
Jvto
/V
/goo
5 "30
Test
:uel
Ht.
DM
2. /
Fl.ue
Draft
(In
0,0 %-
Comments
/O , ~2_ fi-
Combustor Temp.
9-33
-------
ENGINEERING-SCIENCE, INC.
Client iS^A -pfitl.
Date
ES Project |
WOOD IIEATEIl CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Oed
V/ood Heater Model
Operators {
Page
of
i
o
o
l_n
I
CO
I
Time
Sampl 1 ng/
Clock
f^^o
(bt-t)
/fslC>
/6^o
/63>o
/4^o
/fc^o
/1 00
/I/O
/7^^
/730
/7vo
175-0
/B^O
l&tG
l/S/V
Test
:uel
•/t.
(Ibs)
S^
~?.£,
lf.(.f
5.1
V,c/
3,5
Z,7
J^J_
A 6
/r ^
A^
0. 7
<\Q*y5
^^3
O.OV1
0,0 VT.
••
Comments
*
Combustor Temp,
/67o
/A/ 8
ICH2.
JL23_
8-2-7
773
7/7,
Mo
Top
fiZ
Hear
Surface Temp.
52L
53S
5'23
503
llottoni
3-37
3V6
-3V?
37
355
3.^7
RfgTTT
357
3^
Wo
TeTt
212.
1/8
Stack
Temp .
74
5l2_
^77-9
011 .
Tun.
Temp
/•^•z.
10
96
95
Room.
Temp.
_az_
S5?
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC/5
Date
Samf
Samp
Run
Oper
Amb1
- 9- TxC. - S 1
)ling Location ^- d- |
lie Type
Start Time 0 f?>(s± ».
Stc
Prc
p Time
/ 8' *•/ /\
be Length and Type . /^-' ,^/tiii / — V
H^Or- Pi tot Tube Coefficient ,^-r w / J
Number 'CCS - 5S <=— — "3 /V
^ator VAiv\vAt \ ^\ f^V 6^
ent Temperature
Barometric Pressure
Static Pressure, (Ps)
Filter Numben
Meter y
.s)
— . ^^ 7
Assumed Moisture *-/
Sample Box Number A PC^Q
Meter Box
Meter H
Number • A)- /
Pretest Leak Rate ,oo&
//o ( 1 <-/£>
I2£> )I5O
/3o /2oo
,^0 ;2J<^
tfo / 2^-0
/6o /2/3O
( 7o i"2f-
TA5 13 10
•zjo n'^
Z~i° 1^0
~2-?>O 1 5-o
Gas Meter
Reading
(vm) ft3
7,17,0
ttl*°>
7^1-7,0
^"^ZiO
7,-ST, J
:w z.o
?>^/.7i /
352. 2_
-3^-7 2—
'7^6 2, "^
'/VP 7. S
37 2. C
777, 7
78 "2 - S
^>B7, ^
^93.o
o^S.o
V6"^1 1
V^Of ^~
'V / 3' *Y
^/ /^, 'S
V^- 3. Q>
V2Sa *?
V3V. /
Vel ocl ty
Head
( PS). In-
^vO^ ^
£<£>3&
O • o 3&
6, c) T, ^
o.o?, g,
a,o3ft
0.03R
0,0 3 a
^5«- ^ *^ ^
O ^"" *^\ 5<
.o.o^fi
6to3B
^.o'^'B
(5,o 7) ps
(J.o''.^ £s
o,0^ Pi
0 ( O "^ S**,
^,03^;
C.C "S^ •
^^•8
^,c>">, £>
0-G ^ Q,
^,^'7^
Orifice F
Djffere
( H), in
Desired
• "1 5
tc*.v>
0
.95
^^j
i ^^
f *?'S
• 9^
9S
,95
r ^ 'J
.9 -"5"
• S-7)
« c/f>
L 1 ^
( ^S
,75
.rs
. ^5
, 95"
.75
r?*=T
.^•s
, <7 Cj-
,73
,9
^ "^
£ 3
Filter Impinger
7 <-/ dj-S
79 5'5
fvO ^"Q
a 'o 5"?
r? / 6 /
5"S ^3>
^"
^Q, g"2
^5 V jT
51 y- y<^»
P/ 5"7
^/ 5-7
^•-/ j5"^>
8 i- !V?
S"3
^
7_
2-
2_
•^_
?
•2.
7
•2.
2_
Flue Draft
in. H20
-------
Rp=2i£pia
fc,*--*^r-« r^ rr-rw.
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
CC -I
Hood Heater
Date
-1&- ft0)
Sampling Location
Sample Type "2-ti /^G-
Run Number C.C ^ - ^ &
Operator
^ <^>
7*f >
A
f) H
Sampl i ng
time,
Clock Time
24-hr
2
Gas Mater
Readi ng
(vm) ft3
Vel oci ty
Head
UPS) in.
H?0
o < *
Ori fice Pressure
Di f ferential
(AH), -in. H?0
Desi red
Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
2^L
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H20
, o
5
-2,
3 ^
.95-
3
"5
. o ") 8
8?
^L
^ 0-3
_r5.30
"3Vo"
90
330
370
0.0 I
SS'
_Z,
X^j
"Z.
2-
96
ff
,•73
^^
Z_
, 2_
96
30
.o-3 8
L£^
86
o
I
o
n
/73Q
£•£
85
< 95-
9.5'
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
A
Sampling Location
Sample Type_
Run Number
Operator j
\. Clock Time
Sampling\(24-hr
time, min^vQlock)
• — ' __
//&6 /-7^0
LI^G J&oc*
^oc> iBiO
•SoH \Q,H
Soy
Gas Meter
Reading
(vm) ft3
S?T8.0
5"6 ^. /
.T&R ~>
<*7c>. iy^^
•z^'is.vy/
,
Velocity
Head
UPS) in.
H90
o.fc'S-B
o.o -^s
o.o^ ^5
• 03 5f
Orifice Pressure
Differential
(AH), -in. H?0
Desired
.C/S
.95
c?S
Actual
, ^S
.*??
,95'
.flf?
Sq
_
Impinge'r
f?-;
^^
5"8
•
Pump
"Vacuum
in. Hg
•£-.
-?_
Flue Draft
in. H?0
o
I
o
o
Ol
I
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC^
Date
Samp
' 7 ""^*^-U2- — ^" /
iling Location 7)T ^ /
Sample Type
Run
H5r>-
Number CXi.'S - SYv— - cS'"fek
Start Time ^cl-5"e» T Q
Stop Time
Probe Length and
Pi tot Tube Coeffi
Assumed Moisture
Operator l/\)tH4- -.\y^r(A
Ambient Temperature '
Barometric Pressure
Static Pressure, (Pq)
Fi Her Number(s)
Meter
V^-^. \,C>C>£)(f>
| /£iJQ
(fO Ifz^O
•70 ll£>O
So t(io
^O /( £O
'OO (I"JO
DO \\HO
(2,0 llSO
nQ ti,fa
CoD n i*O
lif>O fi-'^G
(7C> ( IMG
\%O , -L^t^.
(^£) 1 2^0
2&G t *•*> t&
~i\e> / •? zo
5>zo /^,tXO
"Z^So ',-^,^0
\ •2." -< o , ^*5^
Gas Meter
Readi ng
^>l 1iOO"i_
"?>( "7'D
32/, 9
7>Z7.o
3?>2.^c
-337.1
7>'rfr7lf
"?>52-- ^~-
357. ;^
7^6 2c 3
•3^ 7--S
^•72.6.
7S2-J?
3ft7, t
•^11 j3
-1 7S -^
'VdS. |
-yop -2_
v/ 1> .-'-f
Z//S-S'
»y 2 '3 v
vx ^. 9
H^'->/' /
Velocity
Head
( Ps), in.
H?0
0.038
<5.O"3>^3
/o. <" "5 V
Oto 3 -° 3 &
o.o',"^-
o^o^f;
d.o"^^
(5,o TJ ^,
. 0.0^?^
Qc<3'3. 8
6 o '3<5
0.07,3
(^^Q^gi
0,038
O^o ^ •
cXd> '3 fi
o.o 3g>
-X
Orifice F
Differe
( H), in
Desi red
,r(S
.95
>
• ^7f5
, "7 "S
( "?5"
^9S
i / J
^'y"?
,95
v^S
,9-S
•^^
. 'v 5
r c/<^
f T *3
. 7S
. *> "S"
'_2i^l_
•ressure
;ntial
H^O
Actual
.^ S
• */ S"
,, 9 ^
_cc^S_
t ?ti
i "75
.?S
.95
- 'S"
.C/S
, ? -^
' ?S
'?sr
.9s
^ 75
, ^^
r 95
'^"S
l^s
. ?s
. "? S
. c~/<)
. ^s
'
SS
fi"7
& ~7
&7
)
rPv
t?^r
^^
^7<7
S"s"
S^?
8" V
r? 3
t^ l^
^3 •— >
2? ^
2 "Ti
r-^ ">.
S 7S
•£ "?
e 3
Filter
•
Impinger
7-V ^Q -
7<^ (J ~2_
/ cy
^ C=
67
/. (JS
vw Ci
<•-/
76
-5-7
"7<£ "5" 7
-7^, ^^
7 <£.
"2_
~2___
2_
"5
"2_
21
o
p
«->
•?__
2_
?
^
Flue Draft
in. H20
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater cT^l - /
Date <7 - "2/, -
Sampling Location £5
Sample Type <$-<•
Run Number C.C. ^ ~
Operator JJ1 c R jfa
-5
J2_
^£
O .
I
Ni
a?
7, 7
, 95
O-o'J-S
99
<±L
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Heater
Vlood
Date <=? --2-
Sampling Location
Sample Type
Run Number
Operator
CCS
10 U- U
^\ Clock Time
Sampling\(24-hr
time, min\£lock)
~~ — — — — __
^e& /-KG
^9o /Soo
Sbo /S/O
•S<5^/ 18/V
( i
Co^f
Gas Meter
Reading
. ^.36
^5-«.V3/
•
Velocity
Head
(APS) in.
H?0
<^.o •? $
d>.o3fi
6. <3 3^
• o-s^
Ori fice Pressure
Di fferential
(AH), -in. H?0
Desi red
, 9?
-95
.9S
Actual
( c/:;>
• v.s
. e/5
»qs
TEMPERATURES
Dilution
Tunnel
1
/
,/
v-
V
qtf.Ts
Meter
In
<7t •
9;
7/
-
Meter
Out
B7
87
a-?
%
\
V
^
•
Filter
So
8*
^0
s
/
-2,
Impinger
60
-5-*?
5'c>
•
Pump
Vacuum
in. Hg
"
-------
FUEL MEASUREMENTS
Date ~'8C) Wood Heater Manufacturer
Project No. Kh 12.:
Run No. C^^i ~ ^»
Circle One: <^
Fuel Type and Amount
Ideal Load Weight
Fuel Piece Length
S
^*- — >— ' X'
Pretest Fuel
2*4
"
/v£,.-'
Moisture Meter Calibration 12%
Wood" Heater Model cc-<-5o
s Test Fuel
r 4x4 1x4
Actual Load Height
/-Z,,^ 22S -z^.o
Moisture Content- (Meter - Dry Basis)- Corv*cTt
-------
FUEL MEASUREMENTS
Date l_
Project No._
Run No.
fN f7.
Wood Heater Manufacturer
Wood" Heater Model
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight
Fuel Piece Length /'-/
4x4
l
1x4
. Actual Load Weight
Moisture Meter Calibration 12%
vJ*o^ T< «,?°F -70
22%
Piece No.
1
2
2
4
icr
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)- Co *•/•«: ltd
Readings Average
2o, 2. ^
2
ZC. "1
2.3.1.
/a.
'Jt Z3.6
- 1^.1^1
Overall Fuel Moisture Average
-2,1, 3
G-CC5-3-24
-------
TEST
CC5-4
UM1381AAPP
-------
.Method 56 Proportionality Rate, Flow Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
1st date: 9-27-89
Run no : CC5-5G-4H
1st time
(min): -190.00
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
210
300
360
420
480
490
Units 1-metric,
2-Engl ish:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hq):
Stack area (m2,ft2):
Wood moist (.'/. uet):
32.60
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
039
039
039
039
039
039
039
039
039
039
stack
temp
(C,F)
85
96
91
95
99
93
98
95
89
88
DGM
rdg
(n>3,ft3)
571.005
601.000
631.000
661.100
691.200
721.000
751.000
781.100
811.300
816.396
Burn
DGM
temp
(C.F)
71
77
79
80
81
82
81
80
81
81
2
0.995
0.99
28.56
30.12
0. 1963
17.94
Samp vol
(sm3,scf)
241.257
Flou rate
(dsm3m,dscfm)
145.59
rate (dry kg/hr):
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
900
900
900
900
900
900
900
900
900
900
vel
(m/min)
(ft/min)
798.23
806.24
802.61
805.52
808.41
804.06
807.69
805.52
801.15
800.42
1.49
PR
(.?.)
102.6
99.6
100.7
100.9
98.3
100.2
99.7
99.4
100.8
dOGM
vol std
(m3,ft3)
29.928
29.599
29.587
29.533
29.184
29.326
29.478
29.631
4.991
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
803.98 92.90
a
i
n
o
<_n
I
4^
I
-------
Method 56 Proportionality Rate, Flow Rate,
burn Rate, and Sample Volume Calculations
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
490
ORVILLE
CC150
ES
9-27-89
CC5-5G-4B
490.00
32.60
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
039
039
039
039
039
039
039
039
039
039
Units 1-metric,
2=English:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (?. uet):
Burn
stack
temp
(C,F)
85
96
91
95
99
93
98
95
89
88
DGM
rdg
(m3,ft3)
571.005
601.000
631.000
661.100
691.200
721.000
751.000
781.100
811.300
816.432
DGM
temp
(C,F)
71
77
79
80
80
82
80
80
80
81
Samp vol
2 (sra3,scf)
1.009 244.807
0.99
28.56 Flou rate
30.12 (dsmSm.dscfm)
0.1963 145.59
17.94
rate (dry kg/hr): 1.49
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
900
900
900
900
900
900
900
900
900
900
vel
(m/min)
(ft/min)
798.23
806.24
802.61
805.52
808.41
804.06
807.69
805.52
801.15
800.42
PR
(JO
102.5
99.5
100.6
100.8
98.4
100.1
99.8
99.3
101.7
dDGM
vol std
(m3,ft3)
30.350
30.015
30.004
29.948
29.650
29.739
29.948
30.048
5.106
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
803.98 92.90
i
o
o
Ol
I
*-
I
to
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED °) - 2 7 -
DATE RETRIEVED °l ~~~LJ~
TEST LOCATION £ $ - LJ 5 -
WEIGHT GAINS
PROBE
LINE
Q ,
SAMPLER SN// "3 V / .
CONDENSATE / f, 6
FILTER#1 /I .T.
FILTER#2 0 ,Q
TORR ABSOLUTE
_(—IN HG) TEMP. 7, / (C)
;. /
POSTTEST B.P.Ttf ,/*? (IN HG)
TANK /(£ , <£ ( — IN HG) TEMP. 2. "Z- (C)
TORR ABSOLUTE 3 V
PRETEST LEAK CHECK
'START_£J3___(IN HdO) FINAL_
POSTTEST LEAK CHECK
TEST TIME V?C (MIN.)
STOVE ID CC-
WOOD SPECIES fie, c.c //} 7
WOOD MOISTURE (Z DRY) £
WOOD MOISTURE (% WET)
WOOD CONSUMED (LB)32,0= (KG)
SAMPLE FLOW RATE PRETEST
ROTMETER £T =(ML
POSTTEST
ROTAMETER
(ML MIN)
(IN H20) LEAK RATE -&. t (IN H20 MIN)
START <-/. y (IN H20) FINAL V, ~7 (IN H2) LEAK RATE Q -I (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
co(%)
02(%)
'~T7
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST
MIN.
MIN.
MIN.
DELTA
5V-/9 PROBE-i-FITTING
9 SAMPLE LINE
CONNECTOR
3 a.
v/
G-CC5-4-3
-------
H./5
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED
-------
CLIENT i
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
I
RUN fto.CCS-OPT-rVfl Placed in Dessicator: Date/Time 9-27'
STOVE MODEL No. TC -
POSTEST
WT 1
WT 2
NT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
ct-t^-W
&e> / ^
q-7/S-*1
yy C)"L,
CALIBRATION WT.
WT AMOUNT =
PRE WT
'V?^
• *y6&
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT £ Pfl
ES PROJECT
RUN \\o.CCS-t)Pr-W Placed in Desslcator: Date/Time
STOVE MODEL No. ^S__
POSTEST
Acetone Lot U V // %
Acetone Sample Volume */ "K
//>
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
J?> 20
%Z35
9 -'1J -^ *?
BEAKER \\
69^ $¥/s
69. <9£>/
ROOM CONDITIONS
RELATIVE
HUMIDITY
^^7^. '
W@~?9~.
-
BAROMTRC
PRESSURE
l£>. /9
3*.o^
Initials
/hc^
snaf
O
O
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
-7
- zr
TOTAL PARTICULATE CATCH (A+B+C) =.
jng.
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
•
RUN ^o.CC6'l)pf-y_0 Placed in Dessicator: Date/Time 9'Z?- 8
V
ES PROJECT #/?
STOVE MODEL No.rr - /
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
r-2-7^
^-z.^5-5
<) - •*?•
// so
3> ^
•/3/^
•>1M
t n~Lv
O.GC^K
BACK
FILTER If
S4£-2~L,
0/10^
* /zoy
a/Z^V
,1-Lll
- O,OOQ~1
CALIBRATION WT.
WT AMOUNT =
PRE WT
, ^a&0
, ^6£>o
.Wl
POST WT
,c>. /
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT £ PA
ES PROJECT KO
RUN N Q.CC5"- £>/>/- V/ff Placed in Dessicator: Date /Time
STOVE MODEL Nn. C.C-
POSTEST
-7
te.
Acetone Lot , oo&dL,
5o.e*k??£>'
-------
CLIENT .
ES PROJECT
J13
PARTICULATE WEIGHTS SUMMARY Page
RUN No . /^ Z Z.
~70-/£>Z.^
7o. ^> 9V9
« oo73
CALIBRATION WT
WT AMOUNT =
PRE WT
5<3 . £>1_
C&.00O/
POST WT
£l - ^>^<3 Z_-
ZG.OOO^
ROOM CONDITIONS
RELATIVE
HUMIDITY
y*®>7*. '
¥$&)-) 2
BAROMTRC
PRESSURE
3^- /9
5o./5"
Initials
^•<=y^
/tk-g
\
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A+B+C)
. (C)
= •23^.3
mg.
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT
ES PROJECT ftD
RUN No. CC £-£<£• f/l Placed in Dess icator: Date /Time*?-- 2-
STOVE MODEL No. C^C - /
POSTEST
DATE/TIME
FRONT
PTLTER il
BACK
LILTER II
CALIBRATION WT.
WT AMONT ~
PRE WT
POST WT
ROOM CONDITIONS
RELATIVE
HUMIDITY
BAROMTRC
PRESSURE
Initials
WT 1
WT 2
Ito
WT 3
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT £ PA
ES PROJECT KD IT-3
RUN No.C^-S'g-Va Placed in Dessicator: Date/Tiine_jm.
P/*y/A><=\ 9-7?
STOVE MODEL No. CC - ) 60 '
Acetone Lot It T // O _
POSTEST Acetone Sample Volume S *&
Z-
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
%!!
9-2^
9-/S-VJ.
BEAKER If
^> o ' Y ^v1
x ^ "7 / C^ "7
Q> Q « CO" O /
X Q" "5 / <7 •>•}
<^> O , ^6i? 5 /
«.«»o
^^/07
CALIBRATION WT
WT AMOUNT =
PRE WT
^&. &t&~£-
"5<3 . £>Q& /
POST WT
5*. oot-L-
$o.o**/
ROOM CONDITIONS
RELATIVE
HUMIDITY
/^>© 7^ '
?&
BAROMTRC
PRESSURE
3<2- /^
^O'C? S"
Initials
/&.*••• jP
ri<:f
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
.0/61
(C)
TOTAL PARTICULATE CATCH (A+B+C) -,
-------
CLIENT
ES PROJECT RD II 3
PARTICIPATE WEIGHTS SUMMARY Page of
(£\
RUN No .CC*>- *>& - V/5 Placed in Dessicator: Date/Time*?- _"? ^^^
STOVE MODEL No. CC - /*7<5
POSTEST
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
4-^9
T-^o .
cy - 2V
//06
9-1^
ns^
9 - / 7^ 2 *)
FRONT
FTLTRR «
^--z;
.?o3^
, 9ol 1-
^o-Li
.%^t/
-£-?3S
.ZZ^*?
BACK
FILTER II
/?£-2~L
,6*$-]
• C151
.(o^-J-L-
„ • c o S 5"
CALIBRATION WT.
WT AMOUNT =
PRE WT
• S^^o
. £o*/
, ^^o^
POST WT
- 9^f *7
, ^"<3(3 O
• ^oo 1
ROOM CONDITIONS
RELATIVE
HUMIDITY
v^@>7/
V^©7.
V./ ^
J-o. /9
3>o.* 5
Initials
a~r/?
/KCJ$
**c£
(A)
(B)
-------
Client _ fc
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
" Run *
ES Project t
Wood Heater Model
Operators [AJ
4-
TEST RUN INFORMATION
Attempted Burn Rate (Kg/hr) !3 Secondary Air Setting A/0
Achieved Burn Rate (Kg/hr } /,
Primary Air Setting
fcW "TC
»iu>-s.
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
Pretest
Post Test
73
A' ./" - /o.
TEST FUEL DATA
/, 5 1-
Firebox Volume (ft-)
Fuel Charge Range Wt. 7.6 to //, "7
Actual Fuel Charge Wt. TOJIL^U)>3
Coal Bed Range Wt. 2.J to Z.S
Actual Coal Bed Wt. Z«7
Fuel H20% Dry Z^i.c
Fuel: Dry Kg | Z.i
Wet
LOADING/TEST START OPERATIONS
By-pass CU-bocy Air Settings
Door ckvsxzaQ. <2i Q^-5^ — Comments
Velocity Traverse
p Temp
A 1 0.033
2 6^37
3
4
Ave.
Pitot Leak Check
Static
G-CC5-4-13
-------
ENGINEERING-SCIENCE, INC.
CHunt £PA -VI fit!
Date
ES Project
WOOD IIEATEIl CERTIFICATION TEST
TEMPERATURE AND I:UEL COHSUMPT10H UATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators
. Page
Time
SampH ng/
Clock
9 5?
t>ct
i A
6S
Test
:uel
•/t.
(Ibs)
0.0
3 .V
Li
Fl.ue
Draft
(In
0,670
0,0 ^C
>ti
Comments
A
A
Combustor Temp.
/v-7
//, /S C
8*8
6TS
fTT-G.
/on
^77
17
57V
3^.0
Surface Temp.
Top Rear Uottorn Right Left
±&L
*/•?/
va/
333
1i-\
i-i!>
3S7
'75?
VZ7-
350
275
^7.5
v/y
Stack
Temp .
Oil .
Tun .
Temp .
3
^L
12.
95
«•$-
8-7
Room.
Temp.
22-
7Z
i2_
23.
25L
73
75"
2SL
2V_
-------
ENGINEERING-SCIENCE, INC.
CHunt £P/)Run I
Date
- 27-S of *?
/? /y
Time
Sampling/
Clock
/7..T-S
/3
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client SP*4 -^fi
Test Fuel Charge
. Page ^3 of 3
Date Q-27-^SV"l Wood Heater Model CCI5O Coal Ded
ES Project, g
Time
SampH ng/
Clock
itel ^
/6ZS
/43S
/^^K
/4?5
'7^^
/7/5
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£>.p^~L
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2 .^ifa
••
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Comments
Combustor Temp.
(^Ti
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V75"
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Temp .
V5^
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572.
(^^^
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Temp ,
7<§
77
T^5
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~7£-
7^
77
77
77
77
7' 7
7C-
76
•7 <1
76
7 1"
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CCS
Date
Samf
Sam):
Run
Oper
Amb1
Bare
Stat
Filt
Mete
; /"""*" ^O -™» ^^ ""s^
*-/ •*" fc- 7 **^ ^d— nr
>ling Location T^r^- 1
>le Type
Start Time
/£5^r
Stop Time
Probe Length and
Type .yz.1/
KSd-' Pi tot Tube Coefficient ,7-7
Number c<^S> — f>d>- — "^X^
'ator i/oUvA , AJ-U.R
ent Temper
imetrlc Prt
1c Pressur
er Numberl
sr X~
ature ' -7-2.
jssure 1 o . / Z. (aJ> //
/?. „ - /.>"
Read and Record All Data Every /O Minutes
Clock Time
Sampling (24-hr
time.min Clock)
2>
/£>55 ISS f>
10 It&S
?j> in^
/'O \~t-t-^f^
I7£> /"2-S£
HO ,!<,<;
mo / 1, f <$
(£>& /'^22-/.O
6iL6>.O
6-31,0
/i "3 6 . /
^ v/* /
^V^. "i-
f o 5 K |
^6 "aftf » \
/jpLP ' ' /
fablt -. 7—
/, ~7/» "i
/; 7<^.. 2_
/c> S1^ « Z.
fc^Cs* 2_
6.11. 1_
Velocity
Head
( PS), in.
H20
<>. 6 s«9
t^.c)-J^
c/ogc/
^.0*3^
0103^
Ci.C'^c/
0,0 •} "I
£>tO"3 t
(!>(O'39
. Ci.c.^^
O.O 3 '?
<5lc.3'=i
O > <5 ^r)
o » 6 39
o . <=> 3, r/
£>f "^^j
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rt . rr •? 9
1 ^o
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' 9 o
^ 9o
. 9 0
, 9o
.^O
•> rl o
• .) ^0
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Actual
clO
.^0
,9o
,9(0
.'rO
."r^
.90
.90
• 4^
I ^C"
.9o
,9o
„ 9 o
/) 9 o
„
7*7
7"r
79
^
^o
S^O
go
Se
b /
^<^
S'o
S'o
S /
& /
Filter
7O
•
Impinger
50. -
7^ ^"7
7Cp
7S'
76
79
7-1
SI
<$!
•5' ?
5*1-
5'Z.
(gb 5'^
S"o 5.' fj
^d ^"£/
Bo 5~y
7V
•79
5V
75 ^^
7^ 5^S
77- 56"
So fsc^
ft /
57
^/ 57
^"2. -^ 7
S^ 2, €> (S~
&'2- f>&
Pump
Vacuum
in. Hg
'X_
~2_
7.
^_
-T__
•2.
-j_
2.
7_
~2_
'2.
7-
2
"2-
'2,
~L
2-
7
7,
tL
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater QC<;
Date 9- 7..1 -\
•A
Sampling Location
Sample Type
Run Number
Operator
l/v
.1 14 U
Clock Time
24-hr
Gas Mater
Reading
ivj-iiL
Vel oci ty
Head
(APS) in.
H?0
Orifice Pressure
Di fferential
(AH), -in. H?0
Desired Actual
TEMPERATURES
Dilution
Tunnel
Meter
In
Meter
Out
_£7_
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H?0
15
766-0
711.0
22L
9o
£iL
82-
8/
*W^
336
"25
-736.0
.96
L2^
5'S
•7^7,0
.96
2_
^^1
.90
7?
_L.
tst
"76&..
0,039
i 7 2-S
0 .
79
3
79
•70
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC _5T
Dat(
Samf
Sami
Run
Opei
Ambi
i f^_ o —7 .c^ cy
)ling Location "TTT" tLy
)le Type
M^?6—
Number cf— ~^6— — *-/ 7^
'ator L^ t\ U .V^Afi.
ent Temperature ' -y~2_
Barometric Prt
Static Pressur
Filter Number!
Meter Y'"- 1. <
:ssure -^ fc£>G>
Start Time /Of>S
Stop Time
Probe Length and
Pi tot Tube Coeffi
Assumed Moisture
Type . /-z,"
cient / 99
/o //OS
2.O 0/5
3o /(2-5
^O I/IS
5O / ' *Y *?"
£>O /^s^
-70 ^2<}$"
flf? C2/5
?£ | ^ -ifi
tOO ;z3S
110 /-2Y«?
1 2-° y 2 s*>
1 ^o I 365
/<-<& ' 13/5
/9o /3?-5
,£p /33?>"
/ 7£> ( 3«-/6
/£? ( -3 55
^£ /"V^S
~?J3C> I *-/'S
'X' ^ ^V 2*:}
o 2.0 f-f3^
2,^0 /w*/^'
"2^>O ( YS^
Gas Meter
Reading
(VJ ft3
t,'7(i>.o
5Jg>^o
£?£&>. o
^> 7/ . cr>
•f??^ o
/a6/'
, /^7, / . O
(i) C^f1 "ti
M? O 1 • ^^
6 J6./
&y/ 4 1
C
6 y>/,"2-
/» 2-/r • Z-
/ --J 1 O
Velocity
Head
( PS). in-
H?0
^.037
^.c-3c/
o.ci.9
(i>. c.^"*
^.^D ^
O.<3-5 v
<5-o5^
Ao39
O.U3^
<5.°39
. G.037
O.o^S
£>,03<)
<^ .^ 3'/
r> . ^30
o . & 39
C.O'A^
C •£• ~*><=\
Orifice F
Djffere
( H), in
Desired
r9($>
,
.")<3
. 9^
. 9o>
, ^r<3
.90
• ^/
."70
<^°
f('O
,96
J *?0
cCt O
.'yO
<-jc>
. ') 0
9 o
f 9n
.9c?
•ressure
intial
H20
Actual
.^(3
.l^i
c Od
( *7O
i ^O
.^o
i ?C>
.^rO
*?&
, *>O
,'?o
,9^
_9 o
> 9^
.. 9o
,9o
, 9,9
, 9 a
• ff 0
' 5 °
• 7O
//6)
TEMPERATURES
Di lution
Tunnel
Meter
In
•11
74-
7"<3
^o
P5 /
S(
&/
c?3
63
£}-^
s^
&3
1
S "5
%y
^)
ft
-------
o
I
n
o
Ol
i
4>
I
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O
S^
o/\
ENGINEERING-SCIENCE, INC.
nrLii'tu uttirt ^LoriL.; o
Wood Heater d-Cf?
Date
<^' - 2- 7 —S> °/
Sampling Location h>7~ **- 1
Sample Type
R^^-
^
Run Number CC1^ - -'<5 VT^
Operator lotf M- . -A >V K ,//'^ £ ^^3-
Sampl
time
.— _
\ Clock Time
ing\{24-hr
, min^v^lock)
~~ — — —
*2,c?O I5o*^
•£40 ^p/*?
7,7o /^^^
2^&O C? 3 S
25>O /"3VS
p^to /55c5
-=s&
-T%
M>65
•> /6'S
t(* 2-5
V^o /^ 3s
35~o ) £.o • /-f^S
HI° ri'-ff
'-/Zc.
^ / 755
3 /(c>. D
7/1,0
-7/4-0
-724.0
77./-0
-73^,^
7 ^/.O
2_^^ • c>
/5/'<^
7% -6
77 » /
7 ^ /' . r>
75?/ . /
'7?'£> /
<^d /, -Z-
^/•Y- .-"?>
Vel oci ty
Head
UPS) 1n-
6.07, 9
c.Q;v)
6«c 3^
6,03^
c>". c -^ c?
A0^c/
(3't
o . o 3^
C?- 'i
Ori f ice Pressure
Di f ferential
(All), -in. Hj>0
Desi red
i '?^
^
, r/<^
. vo
, 9 <^
j "v c^
i c; ^
s ?£
^9 r
« 9c-
/. ?^i
^,^7 f-;
0 7 ^
Actual
, fio
ft(±
.9o
\ct 0
(CIO
• 1°
- 9c3
. -vo
.^o
.9o
. VC
,90
.90
• O^'
, 9'o
-- ?o
/. 9o
. cic-
, 9o
* 9o
/• '/V-v
CQ r>
. 9 ^
i
TEMPERATURES
Di lution
Tunnel
Meter
In
3^ •
ar
f^Ci
RS
Sr,
&<*•
8s
£ v
«?* V
ir^-r'
c?O
5^0
8 <2
^ c
^ic
>ie
to
^O
S'O
^'
/5
7 ^
7 ^
77
77
77
Impinger
£J\j
^C&
s"c;
5 7
S" "7.
<~T
S-7
_T7
•5' ?
^~7
S"p,
^> 9
,-7
->
2_
^>
c
2.
Z.
c
2_
?•
7>
7
7
7
t_
^
"^
•z^
-z.
Flue Draft
in. H?0
^
-------
FUEL MEASUREMENTS
Date ^- 2-^-31 Wood Heater Manufacturer
Project No. &^ 1 2~?^ Wood" Heater Model
Run No .
Circle One: x-fFetest^aeT' Test Fuel
Fuel Type and Amount" --- "2x*__t__ 4x4 1x4
Ideal Load Weight _ ; _ .Actual Load Height
Fuel Piece Length .**>£,'/ _
Moisture Meter Calibration 12% / £, ( _ 22% Z,Z~ f
Moisture Content- (Meter - Dry'Basis)-CorV£cTe.d.
Piece No. Readings Average
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Overall Fuel Moisture Average
G-CC5-4-21
-------
FUEL MEASUREMENTS
*
Date
Project No._
Run No.
Wood Heater Manufacturer
Wood0 Heater Model
/SC;
- ~/
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight___
Fuel Piece Length /<-/
.Actual Load Weight
Moisture Meter Calibration 12%
rz*7
22%
Piece No.
1
2
3
4
5
6
1
8
9
w
11
12
13
14
15
16
11
18
19
20
Moisture Content-'(Meter - Dry Basis)—c
Readings Average
?3,3 23,8
(1.7
4
2-^i I \ i
-------
TEST
CC5-5
WS\RD123.40
RJM1381A.APP
-------
Method 56 Proportionality Rate, .Flou Rate,
Burn Rate, and Sample Volume Calculations
o
i
o
n
Ul
i
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
1st date: 9-28-89
Run no : CC5-5G-5fl
1st time
(min): 530.00
Chrg ut
(Ib uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
530
18.50
vel dp
(mm H20)
(in.H20)
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
Units l=metric,
2-English:
Y, DGM:
Pi tot co:
Gas MH :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (7. uet):
stack
temp
(C,F)
79
80
85
88
86
85
87
87
87
81
DGM
rdg
(m3,ft3)
818.417
848.200
877.900
907.500
937.200
966.900
996.800
1026.900
1057.000
1082. 187
Burn
DGM
temp
(C,F)
72
78
83
84
85
85
85
87
89
85
2
0.995
0.99
28.56
30.12
0. 1963
18.41
Samp vol
(sm3,scf)
257.381
Flou rate
(dsm3m,dscfm)
150.43
rate (dry kg/hr):
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
900
900
900
900
900
900
900
900
900
900
vel
(m/min)
(ft/min)
813.92
814.67
818.44
820.69
819.19
818.44
819.94
819.94
819.94
815.43
85.49
17.640
460.00
1850.00
0.78
PR
(2)
101.
100.
99.
99.
99.
100.
100.
100.
99.
5
9
7
2
0
2
7
3
2
dOGM
vol std
(m3,ft3)
29.661
29.249
28.882
28.926
28.873
29.067
29.262
29.155
24.307
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
818.06 84.50
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu:
Model no:
Lab name:
Tst date:
Run
Tst
no :
time
(min):
ORVILLE
CC150
ES
9-28-89
CC5-56-5B
530.00
Chrg ut
(Ib
uet):
run
time
(min)
0
60
120
180
240
300
360
420
480
530
18.50
vel dp
(mm H20)
(in.H20)
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
0.041
Units 1-metric,
2=English:
Y, DGM:
Pitot co:
Gas
Pb (mm, in.
Stack area (m2,
Wood moist (.7.
stack
temp
(C,F)
79
80
85
88
86
85
87
87
87
81
DGM
rdg
(m3,ft3)
818.424
848.200
877.900
907.500
937.300
966.900
996.800
1026.900
1057.000
1082.142
MW :
Hq):
ft2):
uet):
Burn
DGM
temp
(C,F)
72
79
83
84
85
84
85
88
90
85
2
1.009
0.99
28.56
30.12
0.1963
18.41
rate (dry
DGM dH
(mm H20)
(in.H20)
0.900
0.900
0.900
0.900
0.900
0.900
0.900
0.900
0.900
0.900
Samp vol
(sm3,scf)
260.852
85.49
17.640
Flou rate
(dsm3m
kg/hr):
vel
(m/min)
(ft/«in)
813.92
814.67
818.44
820.69
819.19
818.44
819.94
819.94
819.94
815.43
,dscfm)
150.43
0.78
PR
tt)
101.5
100.8
99.8
99.6
98.8
100.4
100.7
100.2
98.9
460.00
1850.00
dDGM
vol
(m3,
30.
29.
std
ft3)
071
605
vs/VmTs
0.01
29.288
29.
29.
29.
29.
29.
24.
432
181
530
673
511
560
vs ave stack
ave temp
(C,F)
818.06 84.50
o
i
o
I
ro
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED 9~ 7
DATE RETRIEVED
TEST LOCATION
- 1*1 - S"
SAMPLER SN# 9<£?.Z7-
(HG BAROMETER UNCORRECTED)
WEIGHT GAINS
PROBE
LINE _
CONDENSATE
FILTER)? 1 _
FILTER*2
0.7-
70.1
PRETEST
(IN HG)
TOTAL (MG) // 3/« 5"
PRETEST LEAK CHECK
RUN,?
TEST TIME 5~3O
STOVE ID r
(MIN.)
- / , "L
WOO'D SPECIES
//»
^ /» y >V
Y^ 2,2-.S~
WOOD MOISTURE (% DR
WOOD MOISTURE (% WET) t&M)
WOOD CONSUMED (LB) /o.-S
SAMPLE FLOW RATE PRETEST
^ =(ML MIN)
POSTTEST
ROTAMETER
=(ML MIN)
START
_(IN H20) FINAL3-*- (IN H20) LEAK RATE O • C, (IN H20 MIN)
POSTTEST LEAK CHECK
START •/!
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED tf-l'Z- ^^j
DATE RETRIEVED C1 - 2cl <•')
TEST LOCATION g'S'&J $ ~ Aj t
SAMPLER SN// *£
POSTTEST
ROTAMETER & 2-
PRETEST
— /'MT MTM^ /% ^"
= (ML MIN) 57,
PRETEST LEAK CHECK
START 5%7 (IN H@0) FINAL_5V£_(IN H20) LEAK RATE . 7- (IN H20 MIN)
POSTTEST LEAK CHECK
START//, 6 (IN H20) FINAL V, C (IN H2) LEAK RATE Q ,> / (IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
C0(%)
GRAMS MASS AFTER7 FLOWING 0.5 1 pm ..NITROGEN -FOR INDICATED TIME
PRETEST +Z5' MIN.
MIN.
MIN. DELTA
C(T-3 PROBE+FITTING 5V-
CC-/2, SAMPLE LINE
3V.
CONNECTOR
/'
G-CC5-5-4
-------
CLIENT .
ES PROJECT
PARTICULATE WEIGHTS SUMMARY Page _ of _
I
RUN Ho. CC *>- tiPl"£4 Placed in Dessicator: Date/Time_f2^_Z£L
STOYE MODEL Ho.O"
POSTEST
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
q-1o
//, /S
to - T-
to t<;
10 - 1.
1^ -7 ^
«?- /?-2f
FRONT
FTF-TRR It
S^-?3
./69V
*/£2^
^/^^-2_
./^91-
. /Zo3
,oV79
BACK
FILTER It
$/9q$
t/siy
• //9V
,/~lo6>
" -^6/Z
CALIBRATION WT,
WT AMOUNT ~
PRE WT
. V W
. *)0GO
. Vlqct
POST WT
• ^"«-«i "L-
. V7$^
* ^CrJ/
ROOM CONDITIONS
RELATIVE
HUMIDITY
v^
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of
CLIENT L
ES PROJECT f\D
RUN No.<:C5-&W-$X> Placed in Dassicator: Date/Tiine_2_^k
STOVE MODEL No. CC - /<$£> "^/*s.C>,C>0O /
<~> a , 000 /
POST WT
^9/W?
/
V9,^^
^(7 , <3<5^^
ROOM CONDITIONS
RELATIVE
HUMIDITY
vs^W
!TZ^7
^(i^-^
BAROMTRC
PRESSURE
-2.^.9^
Z9,^^
"2-9. ^
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
•
RUN NoXC5jL^jJT/§ Placed in Dessicator: Data/Time 9 - ? <3
ES PROJECT RD
STOVE MODEL No.
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
^- 3>c
)d /^
lo - T-
tt> 1_&
(0 - ~L.
/(, 7^
9-/7- S^1
BAROMTRC
PRESSURE
^
/Hct
o
I
o
o
Ui
I
Ul
I
—I
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of
CLIENT
ES PROJECT RD
RUN NoXTO£^42l5!&_ Placed in Dessicator: Date/Time °> -
•STOVE MODEL No. C.C /£>&
Acetone Lot U_2//Jt_
POSTEST Acetone Sample Volume.
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
Of - 3#
/ "? 2.C"
(6 - 1.
044^
10 - 2-
/^ S6
-
^-/« - U^
BEAKER 11
/> - 5^
<^ ^.^^ 60
^ , 6&HI
6,1 , GO ^7
,(?A& /
S^c«f
me*
nicg
I
o
o
t-n
I
Ln
I
Oo
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
O .
(C)
TOTAL PARTICULATE CATCH (A+E+C) =.
<:• y'"••
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY .-Page
RUN \\o.CC5>- SG'54 Placed in Dessicator:
.of.
ES PROJECT flP II 3> STOVE MODEL No. CC - /
POSTEST
Acetone Lot it 9 // *tf
Acetone Sample Volume ? 3
(-
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
i
TARE WT
NET
DATE /TIME
nt s
10 - -L.
f> " ^f)
Q •- / 5i - ? *i
BEAKER It
^^^^/
/i«.9/^
^^f/^3
6^9.97
o,
CALIBRATION WT .
WT AMOUNT =
PRE WT
V%1Wr
Go ,c>co /
POST WT
V^.99^
W,97??
ROOM CONDITIONS
RELATIVE
HUMIDITY
V*^. "
52^7
BAROMTRC
PRESSURE
v-9.9*/
~~? ^v ^C^o^
<_. / *^ U 7S
Initials
***
i
\
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
. Oft
(C)
TOTAL PARTICULATE CATCH (A+B+C) =
_mg.
-------
CLIENT
EPJL
PARTICIPATE WEIGHTS SUMMARY Page of
t
RUN No .£££-£<£•£# Placed in Dessicator: Date/Time 9-2?
ES PROJECT #0
STOVE MODEL No. CC -
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
<\ - 3,0,
/L^o
10 ~ t~
/O^^
10 - T_.
/(, lO
1-/7- ^
FRONT
FTr.TKR H
X?^-Z3
A 3/^ /
I.Wf
/>•*>**/ 3
(• 3^V3
,6 "7 So
o.^^-i,
BACK
FTF.TER It
/?^-2V
*^zy
»^9^^
^qzV
.6
. 5oo /
POST WT
. V99^
. y^^
• SnO/
ROOM CONDITIONS
RELATIVE
HUMIDITY
v«@7<9
^^67
^2^7
BAROMTRC
PRESSURE
•29.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
.of.
CLIENT
£ P/)-
ES PROJECT Kf) S2 1 STOVE MODEL No.
RUN No. CCS-G6-GB Placed in Dessicator: Date/Time_JLil5_
"*" *>
Acetone Lot If <7//S£ .
POSTEST Acetone Sample Volume
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
r
TARE WT
NET
DATE/TIME
**~3n/0
lo - T-
o 1 *?/^
9-/S-B1
BEAKER It
/;g.<7779
tfS.577*
Aff, 677%"
«-^«
0.^0 ^^
CALIBRATION WT
WT AMOUNT -
PRE WT
*9.9990 /
POST WT
u Q Qoq£j
f_l Q O *f^jQ
• ^^ Jd
V6 ^
ROOM CONDITIONS
RELATIVE
HUMIDITY
K®?* '
*Z@>6?
BAROMTRC
PRESSURE
2.?. &"
-Z<7- 6-X
Initials
/^of
t*icj>
o
I
o
o
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
0/0*8
TOTAL PARTICULATE CATCH (A+B+C) -
_mg.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of
CLIENT ±
ES PROJECT RO
RUN No.CC£l££-^2 Placed in Dessicator: Date/Time
STOVE MODEL No. C.C
POSTEST
WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
^--if>
/&Y^>
/0~ Z_
lo ~*><
lo - ~u
/6l?
10'^' ^
o^>S5>
9-/7- SI "
FRONT
PTF.TRR ii
X?^-?5
/. 35. 7^
A 33ZV
/. -?^9
1 ,32.04
/, 3>z^^
. 6S^3
• Wol
BACK
FILTER II
*)*T- ?6>
.6932-
.6130
*^1>0
.6S1"2-
• Oto*X
CALIBRATION WT.
WT AMOUNT =
PRE WT
.$&>/
. ^000
.^00 /
M*i^^
/*o?
/^C^
v>i^li,
i
n
o
I
I
: *—'
ro
(A)
(B)
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
' " Run / CC^ - 5
ES Project } A..Q
"Wood Heater Model
Operators L^(
TEST RUN INFORMATION
Attempted Burn Rate (Eg/ln ) ClJ> Secondary Air Setting A^ U ^
Achieved Burn Rate (Kg/hr) «115 Thermostat Setting ,/VA
Primary Air Setting 2~2_ Other Settings c/^^P-^
O \ O -s
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (S)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
FACILITY CONDITIONS
Pretest
/c
Post Test
77_
T-C
TEST FUEL DATA
Firebox Volume (ft-)
Fuel Charge Range Wt.
Actual Fuel Charge Ut.
1,52.
to //. 7
Coal Bed Range Wt."Z~'5 to 2
Actual Coal Bed Wt. ^' ®
Fuel H20% Dry Z-Z.5?Wet
Fuel: Dry Kg
. £
LOADING/TEST START OPERATIONS
By-pass
Door
Veloci ty Traverse
Air Settings
Comments
A i
-2
3
Temp
_SfL
B i
86
Ave.
Q.OHI
4 0^0 §"5
3
40^
Pitot Leak Check
Static
G-CC5-5-13
-------
/) --0,o/o &'I
ENGINEERING-SCIENCE, INC.
Client EfW -0^1: Run I
Date
ES Project I
WOOD IIEATEH CERTIFICATION TEST
TEMPEUATUHE AND FUEL COHSUHPT10M DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators
Page
of
Time
Sampl 1 ng/
Clock
0 9
V
o 9
y_o
/|05
Test
Fuel
Wt.
(Ibs)
"7.1-
13:
//*(.*
3, a
l^Z
Fl.ue
Draft
(in
H?0)
0,0 76
a.o-n
0.6.1,7
C.QZ-7
Comments
-7,S
/9
3[
Combustor Temp
A:-'/
7
7C)
"Z O
377
357
V/9
396
Z5V
Surface Temp.
fop| Rear) Dottom'|[light | Left
3SS
2-S2-
-236
7, 5V
'/ 9
3-5-
355-
299
2.79
'2.7 Z
2Z2_
y/9
v/v
17 "7
^^S
T/9
-V-V7
'/
Stack
Temp .
I'/o
sr
Oil.
Tun .
Temp .
^5-
J22.
_7±.
a^.
Room.
Temp.
i;
2^L
75
"7V
71,
2i
7?
23.
2±L
7V
75'
-------
ENGINEERING-SCIENCE, INC.
CHunt CPA-- Vi p-t" Run
Date
ES Project f
WOOD IIEATEIl CERTIFICATION TEST
TEMPERATUUE AND FUEL CONSUMPTIOH DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model
Operators
of
Time
Sampling/
Clock
I1-/ 00
\mc
t'J/0
Test
;uel
Wt.
Ibs)
9,6,
1,3.
fee"?
6. X
3-
Fl.ue
Draft
(In
C.C-1
Comments
Combustor Temp.
<7? V
tf-fiv
tf '5 S
«•&
Hi ght
•25/0
/7
37/
357
Left
'/
-------
WOOD IIEATEH CERTIFICATION TEST
TEHPEUATUIIE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £ Pfl _ Run I
CC 6 - 5
Date *9 - 7 7) - 7)^ Wood Heater Model ('C -/
ES Project I /? f) / Z 3 Operators fr\C/( ^ tf
Test Fuel Charge
Coal Oed
Page J3 of
CD
I
n
n
\>\
\
•In
Time
SampH ng/
Clock
n ^
o
v? :>
0.2-
So
MU.
Test
Fuel
Wt.
(Ibs)
£•0
^L
V.7
V. /
Z.7
A.n
F1.U6
Draft
(In
IlpO)
0,032
0,0-ZS
0.027
o ;,^'
o.ots
0-0-2?
Comments
Comhustor Temp,
•56 y
^y-
^ V
3
<•/
(TVS'
7^3
So /
lop Rear Bottom Uight Left
'(.7
'*'*»
Surface Temp
~i~~ji_i_i~~ i 11 J~"
isy
3? y
39-5'
17?
3.2
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater (~ c /"^CJ
Date
Samp
Samp
Run
Oper
Ambi
"• °) - ~2 3 - S *7
• ling Lo c a t i o n j£ <, CD* c<~S /•/
ent Temperature
Barometric Pre
Static Pressur
sSure
e, (PO
Filter Number(s)
Start Time ' <-* '°
Stop Time /
Probe Length and
Type . /v '- G/*} 5-?
Pitot Tube Coefficient ^ f/^
Assumed Moisture
y"
Sample Box Number /)
Meter Box Number
Meter II
47 /?
/^^, 7>r /T /7
Pretest Leak Rate &r (j / o <& //
Post Test Leak Rate^x^^^ 6^*7"
Meter /^c^o/- £>.'<79y"?
Read and Record All Data Every Minutes At ^ 0 '^3
Clock Time
Sampling (24-hr
time.min Clock)
O 710
/O \~l-~2o
2o 1 ~2'?>O
5*2) /T. y<&
cfo j?_ c;o
_5P /3^>
?o ^-20
fiO V3 3o
% / 3 y o
/to / ? 5b
//o A/V-o
/zo /V/o
,^0 /*i>ZC
/t>o / ^ ~3^j
/Oj /£-/*-//*•
ILO /y <5"^
/7# ^$"^ /&•/&
Gas Meter
Reading
(VJ ft3
t."/' y c^* *^ ^ "7
yttfiff /
\^ f ~?( ^^
^? ~y s<* ^^
^^^y V
fy<& p 7—
'B'S.Bc O
&*;)&• O
Ri '?>.o
,(5(i:& .C
8 7 3. 0
<2 77.*?
2^>2 , ^
G O X^ TO
xp o T ^-)
"B97*. 7
9tf~z. « 7
9r>"7« T
g;^ 5"
9/7 1 5^
9^7. , y
92 7, 3
9 ^2 a 3
^37^ 7__
Velocity
Head
( Ps), in.
H20
C,oi-( /
c . c y/
^ . <:' l//
o , <^y/
d,<^9/
C / c V/
Cv- . C V/
o ,o*y/
&,ov/
o , o'y/
r *-• / /
/*"*! (T^ / /
0,0^/1
c> , c y/
(^\ /** <^v y
Orifice F
Djffere
( H), in
Desired
£ <1&
d 1 Q
< C7c!)
.90
< v <";
- f 0
i^C
,9o
. ?O
3 ^
" 7 9
j '/'o
• 9 e1
tf / ^-^
o 9o
> 9 ^'
. 9^
•ressure
:ntial
H20
Actual
>9<^
•• 9^>
4> 9o
* 9. 9 o
« 9^
'• 9 o
. 9^'
/• 9<3
,. 9 (-,
' 9<^
• 9<^')
^ 7^
•9o
TEMPERATURES
Di lution
Tunnel
Meter
In
7Z-
7S"
73
"»' /
£{•£_
83
*V
S<»
r^Or-
$ c
£1 7
^7
*? 7
5U7
?5 7
S ^
^ ?
S'V
•% ^
3 S
S^ S"
^ ^
^^
^t?
Meter
Out
7 "Z- -
"73
7y
7 5"
77
•7*
7* -
So
&o
,° /
f? "2
?< 3 -
^x "3
•K 3
^ 1
^^L
*%Y
"^y -
y
^>y
fty
^-/
^v
K ^ -
Filter
7/
74
•
Impinger
<^ S
cj" 2__
7^ 5*y
76
76
5(J,
5 -7
74 ^£>
76 5^
77 4o
~l~l Ce t
7fc G 1
TVS £ 7_
?•/ ^ ^,
79 <^3
7^ &^
79 ^i^
^0 ^<^- ,
So ,/> -7
fi'"^ 6 (^
•%•/ 5^
??/ ^"5"
f^<^ ^^
% n ^> ^
%a .^^
Pump
Vacuum
in. Hg
*$—
7__
2_
•^_
j>
T5'^
-^_
-^_
Z.
7
^
"Z-
2-
2-
-z
z.
*2L^_
^_
7
Z
-7
2_
'2.
?-_-
Flue Draft
in. H90
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater (^'/ *;(,
Run Number CC, 5 -
Operator
Clock Time
Sampling\(24-hr
time, min^s£iock)
-Z a
Gas Meter
Readi
1U
ng
ft3
Vel oci ty
Head
(APS) in
o V/
Ori f ice Pressure
Di f ferenti al
(AH), -in. H?0
Desi red
Actual
o
TEMPERATURES
Di lutio.n
Tunnel
Meter
In
Meter
Out
Fi1terIImpinger
Pump
Vacuum
in. Ha
Flue Draft
in. H?0
9V 7
a*?
5s'
5-5"
2-
So
5-5
79
7-
J^L
. R
?3A&
as
7
//« / * 9
» 9
a.
SV
_Z_
J2,
•^^ 9
o
I
o
o
Ui
I
•^//
_2.
c ?..
LJ -JO
/o
9V
00
-------
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Heater
C -
Wood
Date -
\. Clock Time
Sampl ing\U4-hr
time, min\Qlock)
V'775 • — —3&&CL
ySCJ •"?-/&£,
ycj C> 102O
Sert> ~Z <^3O
9/0 "Lo<-(o
<^\o floc£>
•
5 "i rt
Gas Mater
Reading
(Vn,) ft3
/^ 07. i?
/f>t>Tf f)
/o fa 7 -
^v
.([ CJ
A °(o
TEMPERATURES
Dilution
Tunnel
\
^
*6 "3. L
Meter
In
9"2>
9/
ft?
^ ^
(S ?i
\
-
Meter
Out
S ? -
?< ^
O- — >
LJ /
^C
^^
§- ^_
/
f
C^
'
Filter
ft 3
?>/
77
^ r
"7 7
Impinger
5"Z_-
•5V
5/
•>"Z_
S'^Z—
S2_
-
Pump
Vacuum
in. Hg
7 ^
•7
"2 -
"Z-
<^_
Flue Draft
in. H20
I
o
0
t_n
I
01
I
v£>
-------
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
SAMPLING DATA
Sampling Location
Sample Type 7. fr
Run Number a
Pretest Leak Rate <3
Post Test Leak R ate
fry
, po'3
/ ,
Read and Record All Data Every
Minutes
Clock Time
(24-hr
Clock)
Velocity
Head
( Ps),in,
H20
Sampling
time.min
Gas Meter
Reading
(vm) ft3
Ori fice Pressure
Differential
( H), in. H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter]Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H90
0
ot
J2.
7S
73
75
o *
5V
o..<
."70
,9o
.'to
•7? -
55"
ao
90
8.0
Sc.
<3~ /
0 /
_7JL
6-
_S7_
sz.
^77. 9
o
7V
9 c
.96
77
7T
. #<-! )
9
7
O- ^'//
o
72-
59
s-i. 9
v/
«? c-
tSL
79
("ID
6 -20
9/>Z ,5
C
*?.
0 V /
79
•5" 2.
o.o*-//
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood Heater
Date
9- ? 3 - ft
Sampling Location /"5~^-c)
Sample Type 7 gV 5" 9o
5*
•z.
.« o V/
.9 a
9/
c/
S/
JO.
&£.
3S
a
o
I
o
o
Ul
I
ffO
70
I,
7
60
? o
-------
RF^^F^
"feaa *•*--"-
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood lleater_
Date Q-
CC •
/3
Sampling Location_
Sample Type "Z %
Run Number f_ cT ^
Operator f^\c/L
2^.
s-
s -
\. Clock Time
Sampling\(24-hr
time, min\£lock)
"VTo 2^£
V^£> -^ 7~o^<-//
• o<-i /
* 0 V/
»o V/
,r> V/
^>.^v/
Ori f ice Pressure
Di fferential
(AH), -in. H?0
Desi red
-9£>
.7^
« 9 £
/ 9r?
* <7 o
' ^0
Actual
, 9C7
. 7^
• ?o
x ?rj
, 9^
, 9o
^^
T-2-
c- -3
52-
$?_.
S3
•
Pump
Vacuum
in. Hg
?
^
7
7L
7
^
Flue Draft
in. H20
-------
FUEL MEASUREMENTS
Date *?- £S ^°l Wood Heater Manufacturer
.Project No. £p;z,^ Wood" Heater
Run No.
^^— =^s
Circle One: £Pretesi_£«r1 s- Test Fuel
Fuel Type and Amount 2x4 *-/ 4x4 1x4
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length _ (^ _
Moisture Meter Calibration 12% /-2.~<=> 221 2-~-
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content- (Meter - Dry Basis)-
Piece No. Readings Average
Overall Fuel Moisture Average
•
G-CC5-5-23
-------
FUEL MEASUREMENTS
Date V- ^-6y Wood Heater Manufacturer
Project No. ft .ft l~2~~5> Wood" Heater Model_
Run No.
Circle One: Pretest Fuel
Fuel Type and Amount 2x4 <•— ^__^
Ideal Load Weight Actual Load Weight
Fuel Piece Length
Moisture Meter Calibration 125 /~2_ 225
- ^ _ .
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)- CorvwTcd
Piece No. Readings Average
1 2^ Z^_25^ 'L£/.£_
2
3
4
±Z:7_13'7 • 7
Overall. Fuel Moisture Average
G-CC5-5-24
-------
TEST
CC5-6
-------
Method 5G Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE .
Model no: CC150
Lab name: ES
1st date: 10-2-89
Run no : CC5-5G-6H
1st time
(min): 527.00
Chrg ut
(Ib uet): 10.70
run
time
(min)
0
60
120
180
240
300
360
420
480
527
vel
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
dp
H20)
H20)
038
038
038
038
038
038
038
038
038
038
Units l^metric,
2=English:
Y, D6M:
Pitot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.'/. uet):
Burn
stack
temp
(C,F)
86
83
85
85
85
84
84
83
81
80
OGM
rdg
(m3,ft3)
83.202
112.600
142.300
172.300
202.500
232.000
261.500
290.900
320. 100
343.020
DGM
temp
(C,F)
77
83
87
89
89
88
88
87
86
85
Samp vol
2 (sm3,scf)
0.995 247.400
0.99
28.56 Flou rate
29.56 (dsm3m,dscfm)
0.1963 143.59
17.67
rate (dry kg/hr): 0.46
DGM dH
(mm H20)
(in.H20)
0.820
0.820
0.820
0.820
0.820
0.820
0.820
0.820
0.820
0.820
vel
(m/min)
(ft/min)
796.08
793.89
795.35
795.35
795.35
794.62
794.62
793.89
792.43
791.70
PR
Oi)
100.7
101.3
101.4
101.7
99.1
99.4
98.9
98.1
98.5
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
28.
28.
28.
28.
27.
27.
27.
27.
21.
std
ft3)
461
436
513
599
936
987
892
753
824
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
794.33 83.60
o
i
n
o
Ln
I
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
1st date: 10-2-89
Run no : CC5-5G-6B
1st time
(min): 527.00
Chrg ut
(Ib uet): 10.70
run
time
(min)
0
60
120
180
240
300
360
420
480
527
Units l=metric,
2-English:
Y, DGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.7. uet):
Burn
vel dp stack
(mm H20) temp
(in.H20) (C,F)
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
0.038
86
83
85
85
85
84
84
83
81
80
DGM
rdg
(m3,ft3)
83.202
112.600
142.300
172.300
202.500
232.000
261.500
290.900
320. 100
343.022
DGM
temp
(C,F)
77
83
87
90
90
88
88
88
87
85
Samp vol
2 (sm3,scf)
1.009 250.710
0.99
28.56 Flou rate
29.56 (dsm3cn,dscfm)
0.1963 143.59
17.67
rate (dry kg/hr): 0.46
DGM dH
(mm H20)
(in.H20)
0.850
0.850
0.850
0.850
0.850
0.850
0.870
0.870
0.870
0.870
vel
(m/min)
(ft/min)
796.08
793.89
795.35
795.35
795.35
794.62
794.62
793.89
792.43
791.70
PR
100.8
101.3
101.4
10L6
99.0
99.5
99.0
98.0
98.4
85.49
17.640
460.00
1850.00
dDGM
vol std
(m3,ft3)
28.864
28.838
28.916
28.950
28.279
28.383
28.288
28.095
22.095
vs/VmTs
0.01
*
vs ave stack
ave temp
(C,F)
794.33 83.60
n
i
n
\j\
i
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
•DATE DEPLOYED /b - "Z-- S ^
DATE RETRIEVED /0~"2> - S1 ^
PROBE
LINE
- -z../
TEST LOCATION £ S ~ 6J 5 ' £
SAMPLER SN//Q6Z
COMPENSATE 73/6
FILTER* 1 5 Z,7
FILTER//2 / , /
(HG BAROMETER UNCORRECTED)
PRETEST B.P 29.£? (IN HG)
TOTAL (MG) /Z*T. V
TANK "2 9.?$' (--IN HG) TEMP.-?,/ (C)
TORR ABSOLUTE Ib &
POSTTEST B.P.-Z9.7 1. (IN HG)
TANK
(—IN HG) TEMP.
(C)
TORR ABSOLUTE
PRETEST LEAK CHECK
JO
TEST TIME 5'Z-"7 (MIN.)
STOVE IDCC.
WOOD SPECIES Q0^f / ^ <
WOOD MOISTURE (Z DRY) ~Z
WOOD MOISTURE (% WET) I
WOOD CONSUMED (LB)
(KG)
START
POSTTEST LEAK CHECK
START//, S (IN H20) FINAL
SAMPLE FLOW RATE PRETEST
ROTQHETER 6V =(ML MIN)_
POSTTEST
ROTAMETER <^ / °(ML MIN)
(IN H30) FINAL 7.^ (IN H20) LEAK RATE Q .
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED /tf - Z - g °f
DATE RETRIEVED /C) " "*> ~
TEST LOCATION^"?- b)S -
SAMPLER SN//
WEIGHT GAINS
PROBE
LINE
CONDENSATE
FILTER//1
FILTER#2
RUN)? CCS- O
fl
TEST TIME 5Z-"7 (MIN.)
STOVE ID
WOOD SPECIES
(HG BAROMETER UNCORRECTED)
PRETEST B.P 27. £> 1 (IN HG)
TANK 7.9, *T< ( — IN HG) X£MP.
TOTAL (MG) f~2Qf /
WOOD MOISTURE (% DRY)
WOOD MOISTURE (% WET)
TORR ABSOLUTE .S ><->
POSTTEST B.P. 29. 77. (IN HG)
TANK /7. V
-------
CLIENT .
ES PROJECT ftD
PARTICULATE WEIGHTS SUMMARY Page of
»
RUN No.CC$-l)PZ-6A Placed in Dessicator: Date/Tiine.&L^:L
STOVE MODEL No. CC -
POSTEST
••
' NT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/^-y
// f&
\o-H
IT^C*
16^9
r^lT
9-/^-SS
FRONT
FTLTKn It
5/9^-3^
« /70/ /
CALIBRATION WT.
WT AMOUNT =
PRE WT
,^f99
t £)0GC>
f ^PC'O
POST WT
« f«3<5/
« ^OO /
, ^OOC'
ROOM CONDITIONS
RELATIVE
HUMIDITY
$*@>6<*
«&6> «
yo®1o
BAROMTRC
PRESSURE
29«S^
Z9. 7S
'27- S^
Initials
i
>KC^
S*Cj
1 • "
^/c
(A)
-------
CLIENT E P f\
ES PROJECT ftD I
PARTICULATE WEIGHTS SUMMARY
RUN N
Page.
.of.
STOVE MODEL No. CC* /
POSTEST
in Dessioator: fiat.e /Time /O- "?
ftp'/rc. lo -3 ^
Acetone Lot ti 9// ^
Acetone Sample Volume ^/ ;>
/6
7/5
WT 1
WT 2
WT 3
WT 4 -
WT 5
FINAL WT
(
TARE WT
NET
DATE/TIME
10- ^
//3S
/6-V
/7<^
9-/ff-*'5
BEAKER )l
^-3^
/,<5^5SS6
^ ^ . 5^5 y
6tf. ? 55V
^ •g.V'S'/^
c^ f o 7 3 ^
CALIBRATION WT
WT AMOUNT =
PRE WT
^&'f>00 t
POST WT
W,m°\
^o ,ooo1^.
ROOM CONDITIONS
RELATIVE .
HUMIDITY
^^%:
V5<^^^
BAROMTRG
PRESSURE
-29. #r
Z*?- 75
Initials
^ c^
f^c A
o
i
n
n
Ln
I
(BLANK CONG. ) x
(ACETONE- SAMPLE)
WT GAINED
7
o c< / /
TOTAL PARTICULATE CATCH (A+B+C) =.
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
I
RUN No. CC 5- OPJT-/3A a c e d in Dessicator: Date/Time /0-3 @e>
STOVE MODEL No.
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/6-V
II 10
/a-y
f •> ^o
/«-•>-$•
/•^^s
9^/7-^^
FRONT
PTr.TRR It
Ste-i*?
*/75?
W7?/
*n\'^
o r?/3
./Z/6
0.0^7
BACK
FTF.TRR It
5^^-?^
»/i/3
. /2,/T.
« /7./Z-
./l/<9 /
rf 5"^>t>/
a 5of-O
ROOM CONDITIONS
RELATIVE
HUMIDITY
50&6 <&
tf*@6*
fr ®~>o
BAROMTRC
PRESSURE
-29. 9/
Z9, 75T
29. ^f
Initials
t
/X^/?
y^» c/?
M<%
(A)
(B)
-------
PARTICULATE WEIGHTS SUMMARY
Page.
_of.
CLIENT
RUN No.
ES PROJECT HP /23
in Dess icator : Date/Tiine7
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
f
TARE WT
NET
DATE /TIME
to- v
//3^
to -V
n**
°l-/%- 8*7
RRAKER i!
/> -39
7^5 , /6 -L X
7o. ^^
7o^ /'6Z7
7^ . ^ 9 5 ^
O , 0 6 7 cf
CALIBRATION WT
WT AMOUNT -
PRE WT
^T.3, 0ac,t
5 & • e)60~l-
POST WT
V9,99f9
5<9.«5<3dl,
ROOM CONDITIONS
RELATIVE
HUMIDITY
<-<^W
V5^W
BAROMTRC
PRESSURE
•z?. ^^
Z7- 75
Initials
/>1^^
^c^
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
7
TOTAL PARTICULATE CATCH (A+B+C) = // ?„ */ mg.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT"
RUN No.C££:
ES PROJECT /?/? St-^> STOVE MODEL No.
POSTEST
Placed in Dessicator: Dat.R/Tirna Jt> - "% **
£>xf y ,» - /^ - ~>
Acetone Lot it 9// S^
Acetone Sample Volume ^» O
•
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
r
TARE WT
NET
DATE/TIME
)o- y
// 35
16- £>&/
f^C ,066 ~2_
POST WT
^^,9^*)
S<3,«3i3^^>f
^
(BLANK CONG. ) x
(ACETONE SAMPLE)
WT GAINED
0 , cro "*>
(C)
TOTAL PARTICULATE CATCH (A+B+C) =.
-------
CLIENT
ES PROJECT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No. CCS'5(r-^Placed in Dessicator: Date/Time /V-* - ? <^ / 2 V «y
STOVE MODEL No. .rJ,*
lo- ^
)01^
9- /7-S9
e
FRONT
FILTER 11
4*~-3S
).)Z\5
i. /26o
\*H1(t>
/>/-LlS
. /.//76
,6S/7
o.V.359
BACK
FTI.TF.R It
^-?6
>^^7^
, ^£73
,6 S 7 -a,
.673?
J s otj'tt?
CALIBRATION WT.
WT AMOUNT =
PRE WT
,y^<3
. Soo/
* 5"<=t)"z_
. ^ a GO
POST WT
* *;>000
• $ & QQ
f^tvt'O
>£«<>{>
ROOM CONDITIONS
RELATIVE
HUMIDITY
$*&£*
V 5-<*P><£ <#
*fo@7o
v%^,^
BAROMTRC
PRESSURE
z?. ^y
^"7.7^
27^ ^V
Z9- >^
Initials
,
XH<*xf
^c/?
X/cx?
^o«;^
(A)
(B)
-------
CLIENT;
ES PROJECT /?/? /Z 3
PARTICIPATE WEIGHTS SUMMARY Page
RUN No.&^~^"£- ~6 B Placed in Dessicator:
STOVE MODEL No
POSTEST
of.
Acetone Lot U
Acetone Sample Volume
- 7
WT 1
WT 2
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
,/ & - y
/-? Eo
/•v / O C?" ^-i
*-T — / O "" O /
BEAKER It
yX O* // ^~ / X
(^ t? " r ^ / Cx
(r%. % . yv %y
O.c^^
CALIBRATION WT
WT AMOUNT -
PRE WT
^>6,000/
^>O , 606 7_
POST WT
t/tj cjqc)
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
, o o 3
O
.
(C)
TOTAL PARTICIPATE CATCH (A-i-B+C) =
rng.
-------
CLIENT
PARTICULATE WEIGHTS SUMMARY Page of
I
RUN No. rC?-^-'^Placed in Dessicator: Date/Tiine_/2j_
ES PROJECT /? O /2 3
STOVE MODEL No.
POSTEST
C -
WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/a-*/
1/06
lo - 9
I~>-L<>
lo - $
n lo
10 -6>
MIS
q~/7~ 39
FRONT
FTF.TER it
/^~-37
I,tl9*
/'/3W
UU95
/.M33
JjLL^ZS
.67^7
O.V^o^
BACK
FILTER II
^- 3 ^
37
. ^«iK
.^^31_
.6<«r?l.
,67VS
(0* ^ ft) 1
a SobQ
POST WT
. fT<06<5
• ^ aoO
f *>&&-&
• -506 O
ROOM CONDITIONS
RELATIVE
HUMIDITY
$G&6<%
v. ^^
2?. 7 S
a9> sy
2^>7V
Initials
,
/^c/j>
^Cx^
/H <"^
/^ ^yf
(A)
(B)
5
I./Z*/
^ooo *
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
" Run / CC: -
ES Project #
Wood Heater Model
Operators /\
cc
TEST RUN INFORMATION
Attempted Burn Rate (£§/**•-) cL^ Secondary Air Setting A/0
Achieved Burn Rate (Kg/hr)
Primary Air Setting
Thermostat Setting
Other Settings
^»-°r
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (>)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
"70
Post Test
"2,0
/o.o //o-O
TEST FUEL DATA
Firebox Volume (ft-) _
Fuel Charge Range Wt.
/>5 2
to
Actual Fuel Charge Wt. /£>i"7
Coal Bed Range Wt.<^
Actual Coal Bed Wt.
Fuel H20% Dry ^
Fuel: Dry Kg
to
Wet
1) '
By-pass
Door
Veloci ty Traverse
p Temp
A 100)32- /00
LOADING/TEST START OPERATIONS
f Air Settings
Comments
2
3 0,0^ 2.
B i
2
Ave.
3^0. 93
4 ^32,
Pitot Leak Check
Static
G-CC5-6-13
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client ^JPv - VJ ^T Run g
Q ^
Date
ES Project. #
Wood Heater Model CC
^ Operators (,Q }-/
Test Fuel Charge
Coal Ded
. Page
/
of
o
I
o
o
01
I
Time
SampH ng/
Clock
[010
(NO
Test
Fuel
Wt.
(Ibs)
3
Fl.ue
Draft
(In
,0.0
6.0 VA
Comments
-t ^ s t-
IliQ JuW/
Coinl)ustor Temp.
707
STI
V37
27?
229
Surface Temp.
T^]TnTeTrTTlort7oirTRiliTrrTeTt
-/.YE.
***•/
is,-?
e-v?
'67 Z
Stack
Temp .
S'2-7
'3/6
-Z-2 /
Z32
on.
Tun.
Temp .
^H
/^V
SV
Room.
Temp.
2Z
zi.
79
So
&
77
77
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client £
Date /
Run X c" C
Wood Heater Model
ES Project. H -ft f) /?! 3 Operators
Test Fuel Charge
Coal Bed
_ • Page "2^, of
Time
Sampling/
Clock
A/35T
/-?
Test
Fuel
Wt.
(Ibs)
7*J_
•<">
3.0-
•7 ,
Z. 2
Fl.ue
Draft
(In
0/2LO
oOlO
vQ'2.0
Comments
Coinbustor Temp.
H-2.7
-7
lop
2iZ
zsz.
•zn
Rear
Surface Temp.
25V
299
ZV;
Bottom
•27V
2^,5-
26. »•
2.6 S
282-
Ri gnt
? 3
239
Z56
26 Z
66.1
Z6.C.
22^.
272
.eft
233L
27T
7V1
2VJ
•2ft i.
Stack
Temp .
2.V7
25-9
259
^5?
2*5
Z75
275
Oil.
Tun.
Temp .
JS^i
55-
as
Room.
Temp.
-79
79
22.
2Z.
79
22.
79
So
So
SO
29
7?
ZS.
-------
ENGINEERING-SCIENCE, INC.
CHunt lz PA Run I
Date \0 -
ES Project I
WOOD IIEATEIl CEUTIFICATION TEST
TEMPEHATUUE AND I:UCL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Ded
__ . Page 3 of
Wood Heater Model
_/Z3 Operators
Time
Sampl 1 ng/
Clock
/R/S
/V?
Test
Fuel
Wt.
(Ibs)
i2
A 5
6.6/E
/.o
°O-
0.1
6, S
0-0
Fl.ue
Draft
(In
H?0)
.o^o
aoiS
Comments
Combust or Temp
£2-1
V/2.
3^7~
^7Z>
lop Kear Dottom lugnt Left
33
339
7/8
z/2
Surface Temp.
3/7
3V?
30^
270
25' "
Z-9^
SE
?7d?
232.
^73
ZV2.
2.7
Stack
Temp .
2J2.0
Oil.
Tun .
Temp .
as
£i
s/
Sb
ao
^fc
Room.
Temp,
So
7?
^L
55
7-7
7-7
-------
ENGINEERING-SCIENCE, INC.
Wood Heater C£. S
Date if\ _•? -
SAMPLING DATA
Sampling Location
Sample Type
Run Number
Operator
Start Time
Stop Time
Ambient Temperature_
Barometric Pressure
Static Pressure, (P^
Filter Number(s) ~
Meter r •=-"~^
Probe Length and Type_
Pi tot Tube Coefficient
Assumed Moisture ~
Sample Box Number
Meter Box Number
Meter H
Pretest Leak Rate G+oot. &J
Post Test Leak Rate O.OQ-?_ ^
Read and Record All Data Every J6 Minutes
/C"3
Clock Time
(24-hr
Clock)
Velocity
Head
( PS).in-
H_2p
Sampling
time.min
Gas Meter
Reading,
Orifice Pressure
Differential
( H), in H?0
Desired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue Draft
in. H90
rt
//>
0,
ii
So
!iX
5V
"Z-
So
<*-*> *
JLO.
//7. 6
^^.
9,0
7-
loo
5-7
.o
57
-7
3^.
57
7
-Z-
-
55 Z,
JZ
92.
"2-
9V
y
5V
0
:"*o
z
Q 3 Tf
-z
7,
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Vlood Heater
Date
/£> - 7- ~
Sampli ng Location_
Sample Type "2 %
Run Number_
Operator
£f 5
A
Cl
Sampl ing
time, min
ock Time
24-hr
lock)
Gas Meter
Readi ng
(v) ft3
•267.3
Veloci Ly
Head
UPS) in.
H?0
Ori f ice Pressure
Di fferential
(AH), -in. H?0
Desired Actua
TEMPERATURES
Di lut ion
Tunnel
Meter
In
Meter
Out
Filter
<9 a.
Impinger
Dump
Vacuum
in, Hg
Flue Draft
in. H20
. 1
o,
97.
92.
5-7
z,
_5iZ.
? ^
JL
'2-,
9-2,
^L.
6.0 3
e/
ft*
9?
/• 3
.8 7,
•ez
g^.y
.a ^
S-7
WO
s
0,03
8
-e-?
7?
,8
SG
7*7
7?
GO
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
Sampling Location
Sample Type '
Run Number
Operator
h-
^X. Clock Time
S amp ling\(2 4-hr
time, min\£lock^
~ ~ — " — — — —
y&o 2jco<;
l*to Toi.S
£00 '267.?
5(0 >0 3*5.
^lA 'Z.OH^
5Z7 -Z&^t
SZ-7
Gas Hater
Readi nq
(vm) ft3
^^ov(
?>2.5.0
^^7,*?
^7>^'7
•^7,9. 6
^3,010
iX'i.i/K
Velocity
Head
(APS) in.
H20
o.^^
e>-o -^ £
e>.c3^;
o.oi, «g>
C?
AR
\
?«v
-
Meter
Out
56,
R6
c^G
e
7^
7^
Impinger
^0
£o
<2-O
60
<2
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater Cc ^
Date
Samp
i /c - 2 - ^ ^
ling Location r^T u /
Sample Type
Run
H\^ (Sj-
Number CCS - (1>T^
Start Time /7-^S"
Stop Time
Probe Length and
2.^<5"2_
Type . /£,'>
Pi tot Tube Coefficient ,9^
Assumed Moisture
Operator Lx^VVv^ , -^rvft
Ambient Temperature v
Barometric Pre
Static Pressur
Filter Numben
Meter \
;ssure
^e, (Pq)
s)
''-^ /, £>o Gcb
V
Sample Box Number 7^
Meter Box Number
'? /~t?
//TO ^ ^ £>*>
/Qn S^>/4'
2C& /S'ZC
/ c~ *%. t~
iZ<2> /< 5V«^"
1 ^ ^?o y T^<
-2-VO X«£.«T
Gas Meter
Readi ng
(vm) ft3
'RSj 7-
9,3. 0
97, S'
//i 7^ 7
1/7} a <&
_/?Zc-lS"
y^, "2^T
/3'^ , y
/•^7. 3
/yT, "?
y^2< "•?
1 £>")<, 13
/6>? . v23
/fj")*. -3
y72. >3
/77,^
>?5*>v
/ 9 2. . V
"ZoZ- ^
Velocity
Head
( Ps)Jn-
<5i^i'3 ^
O*^^ ^
0,^^f<
^o"^ 5<
« ^ 'a-
« ^> °5 ^
^^ '^ ^
/s c7 "3 3" '
o /? 3 S*
A/O '^ S'
^ o "^S"
a ^, -^ x
* o! S Sf'
„ &-?,'g'
Orifice F
Differe
( H), in
Desi red
. 8^
ressure
;ntial
H20
Actual
.^ 2S-
^, « ^"^
« 8 ^
, % 5
j ssr-^r
TEMPERATURES
Di lution
Tunnel
Meter
In
-1 7
So
<£
^ 7
8 S'
S9"
89
9Z-
c —7
^3f '7
^ -5
9^
*9V
*7 *V
°$¥
^v
jaj*/
'•? ^-
Meter
Out
•77
79
g"Z_
S 5
R "^
S'/^
§5"
3<^
•^4,
^ 7
$7
*? ^
3 S^
S 5"
<-, C3
y /
5^9"
9rf
9^
9o
9
% /• 5"
^2~~
2_
"7
•z_
"2,
•7.
•2
T7
V
•?
-p
~i
"32
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater CC-i
Date
- ?- -
Sampling Location ^ ^ - u) S
Sample Type ~z ft / R
%T
^
Qg
-7
92.
390
£•.01$
9?
-79
7.
.Pi '
-22-
as
4^
o
I
o
o
Ol
I
o^
I
NJ
9
-^
77
/1S5
71
S?
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater_
Date
Sampling Location
Sample Type
Run Number
Operator U
-v>
3/3
\. Clock Time
Sampl i ng\(24-hr
time, min^^lock)
~ — ' — ^
tfBO "Zoos
Y<3<0 2o i*$
J550 -33 ZS
£/3S
^CJ '2Gf-fc2_
5^7 zo^a.
^X9
Gas Meter
Reading
(vm) ft3
'V^-/
^20,0
3^^
33V.-?
3^,^
3V3.0ZZ
/
7
V
Z5?.^o
Veloci ty
Head
UPS) in.
H?0
?
^7
-fr-7
0,f>~)
TEMPERATURES
Dilution
Tunnel
/
\l
V
•5 "i.-7
Meter
In
<59 •
Pfj
•&/
<59
^
-------
FUEL MEASUREMENTS
Date (d"Z-QU 0
Project No. fc.\M2^> Uoocf Heater Model
Run No.
Circle One: <^rret&Tt Fii^l Test Fuel
Fuel Type and Amount 2x4 \^s^ 4x4 _ 1x4
Ideal Load Weight _ ; _ .Actual Load Weight
Fuel Piece Length _ £ _ . _
Moisture Meter Calibration 12%__/7_ _ 22% _ "Z- "c!_
vJ«cd r< * ?. °F ^~
Moisture Content-(Meter - Dry Basis)- CorvgeTed
I
Piece No. Readings Average
2
3
4
5
6
1
8
9
10
11
12
13
U
15
16
17
18
19
20
Overall Fuel Moisture Average
G-CC5-6-23
-------
FUEL MEASUREMENTS
Date /^ - "Z-^7* i Wood Heater Manufacturer
Project No. R frs \ 2_-"!S Wood" Heater Model
Run No.
Circle One: Pretest Fuel _^ T 22%
"
6
1
8
9
10
11
12
13
1*4
15
16
n
18
19
20
Moisture Content-(Meter - Dry Basis)- Co»v*cTed
Readings Average
Overall Fuel Moisture Average
G-CC5-6-24
-------
TEST
CC5-7
WS\RD123.40
WM1381AAPP
-------
flethod 56 Proportionality Kate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: ES
1st date: 10-9-89
Run no : CC5-56-?fl
1st time
(rain):
Chrg ut
(Ib uet):
run
time
(rain)
0
60
120
180
240
300
360
120
480
540
560
560.00
Units l=metric,
^English:
Y, DGM:
Pitot co:
Gas
Pb (mm, in
Stack area (m2
Wood moist (?.
20.60
vel dp
(mm H20)
(in.H20)
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
stack
temp
(C,F)
77
77
78
82
83
7?
80
86
89
84
83
DGM
rdg
(m3,ft3)
344.001
372.800
402.300
432.400
462.300
492.500
522.600
552.700
582.800
612.900
623.081
MU :
. Hg):
,ft2):
uet):
Burn
DGM
temp
(C.F)
67
75
78
79
83
81
79
76
84
84
84
2
0.995
0.99
28.56
29.94
0. 1963
18.19
rate (dry
DGM dH
(mm H20)
(in.H20)
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
Samp vol
(sm3,scf)
273.046
85.49
17.640
Flou rate
(dsm3m
ko/hr):
vel
(m/min)
(ft/min)
752.87
752.87
753.57
756.36
757.06
752.87
754.97
759.15
761.23
757.76
757.06
,dscfm)
138.96
0.82
PR
(2)
98.0
99.0
101.1
100.1
99.1
100.3
101.5
102.1
99.4
101.1
dDGM
vol std
(m3,ft3)
28.777
29.037
29.462
29.212
29.288
29.299
29.407
29.572
29. 137
9.855
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
755.98 81.45
o
i
o
o
Ul
I
-------
Method 56 Proportionality Rate, FIou Rate,
Burn Rate, and Sample Volume Calculations
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
560
ORVILIE
CC150
ES
10-9-89
CC5-5G-7B
560.00
20.60
vel dp
(mm H20)
(in.H20)
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
0.035
Units 1-metric,
2=English:
Y, OGM:
Pitot co:
Gas MW :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.?. uet):
Burn
stack
temp
(C,F)
77
77
78
82
83
77
80
86
89
84
83
D6M
rdg
(m3,
344.
372.
402.
432.
462.
492.
522.
552.
582.
612.
623.
ft3)
001
800
300
400
300
500
600
700
800
900
082
DGM
temp
(C,F)
68
75
79
80
85
81
80
80
86
85
85
Samp vol
2 (smS.scf)
1.009 276.211
0.99
28.56 Flow rate
29.94 (dsm3m,dscfm)
0.1963 138.96
18.19
rate (dry kg/hr): 0.82
DGM dH
(mm H20)
(in.H20)
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
0.850
vel
(m/min)
(ft/min)
752.87
752.87
753.57
756.36
757.06
752.87
754.97
759. 15
761.23
757.76
757.06
PR
(.?.)
98.0
99.3
101.2
100.1
99.0
100.5
101.6
101.6
99.3
101.2
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
29.
29.
29.
29.
29.
29.
29.
29.
29.
9.
std
ft3)
127
445
821
568
591
711
766
766
439
977
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
755.98 8L45
o
i
o
o
l_n
I
—1
I
to
-------
ENGINEERING-SCIENCE. INC.
DATA SHEET YPI IN-SITU TEST METHOD
DATE DEPLOYED fp ^ o.g-V (IN HG)
TANK /^- . 3O _ (—IN HG) TEMP. "2- ~L, (C)
cc <; - u fir - 7 /5
TEST TIME 5/Jt) (MIN.) '1?33
STOVE IP C C /
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED / /> - 9 - 8 ^
/
DATE RETRIEVED /.' 'C '':
WEIGHT GAINS
PROBE
LINE
Z.7
TEST LOCATION j- 5-
COMPENSATE <-{ ^ , O
^ FILTER// 1 3*7 .V
SAMPLER SN//
Z ? V
(HG BAROMETER UNCORRECTED)
PRETEST B.P 7^-5 ~? (IN HG)
/JOJL TANK
FILTER//2
TOTAL (MG)
0.7.
(—IN HG) TEMP./9 (C)
TORR ABSOLUTE V • 5
POSTTEST B.P. 3<^. &*•/ (IN HG)
,y6
''L0 TANK I6?,C,Q (--IN HG) TEMP.'^'L. (C)
TORR ABSOLUTE "3 V / . V
PRETEST LEAK CHECK
RUN//
TEST TIME 560 (MIN.)
STOVE ID Cr / 5o
WOOD SPECIES_
WOOD MOISTURE (%
WOOD MOISTURE (% WET)
WOOD CONSUMED (LB) 7£
SAMPLE FLOW RATE PRETEST
ROT3HETER_
POSTTEST
ROTAMETER
=(ML MIN)
START
(IN HSO) FINAL ^^ (IN H20) LEAK RATE
-------
CLIENT £Pft
ES PROJECT
/23
PARTICULATE WEIGHTS SUMMARY Page
c
RUN No. CCS^BL -7^9 _ laced in Dessicator:
STOVE MODEL No. #K~^T^ CC~/$G
POSTEST
_of.
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/6- If
®> lo 1o
/o-//
/(>o
?-/7^c7
FRONT
FTF.TRR It
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• mco
* W5V
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./3/ ooo
, <^&c> /
t <~?6
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. *> 06 /
. <5&6<3
. 5 oe
-------
PARTICULATE WEIGHTS SUMMARY
Page.
CLIENT
ES PROJECT AD
RUN No. CCG-UPf-WPlaced in Dessicator: Date/Tiine/a^
*
STOVE MODEL No. C C /
POSTEST
Acetone Lot it_*3
Acetone Sample Volume_2_ZL
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
r
TARE WT
NET
DATE /TIME
[ o - //
lt> H $
/^ -II
//„ y^
/& - /z.
; ^10
9- -ao^9
BEAKER it
£7
ff/.2.£»
«/.2S 5-3
^;. ?s V9
« /, 25V9
% / . /99V
o, o ^^S
CALIBRATION WT
WT AMOUNT -
PRE WT
$ £> , O 0 £>£>
V7, 9W
^C3 , OW /
POST WT
5". /y£>C~^
V f , ?'??I8'
5"r>- e«>o/
ROOM CONDITIONS
RELATIVE
HUMIDITY
W^67.
V^^^
V^7/
BAROMTRC
PRESSURE
^^7^^
29. 87
-T-^,97 .
Initials
y>7C^
/>i<^
I
o
o
Ln
I
—I
I
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
(C)
TOTAL PARTICULATE CATCH (A+B-MJ)
_mg.
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of.
CLIENT £Pfl
ES PROJECT /? D /23
RUN No.
: laced in Dessicator: Data/Time
STOVE MODEL No. •
POSTEST
' WT 1 !
WT 2 !
WT 3 [
WT .4 j
! i
FINAL WT
TARE WT
WT GAINED
DATE /TIME
lo~ll
lo ?>o
lo-tt
l(, rt ^
q-n^°i
FRONT
FTf.TRR )»
5/P^^7
> /^/z
./£!$•
,/^/-L
•« x z / %-
<5,o 39V
BACK
Plf.TER it
J^f--5^
« /Z/V
* X2./o
./7./V
./z/z.
£>. a-ts£>~i-
CALIBRATION WT.
WT AMOUNT =
PRE WT
, $06 a
• *5&t>/
POST WT
. $06 /
. 5 o\r /?.
(A)
(B)
-------
CLIENT
P /)
PARTICULATE WEIGHTS SUMMARY ' Page of
RUN N o. CC-S- ffif- 7/3 Placed in Dessicator: Date/Time_/£_l
ES PROJECT R D
STOVE MODEL No. CC - /
POGTEST
Acetone Lot 1t_
Acetone Sample Volume.
WT 1
WT 2
WT 3 'j
1
WT 4 •
WT 5
FINAL WT
f
TARE WT
NET
DATE /TIME
}0 -//
!/>*/*>
JO- II
ftW^
)o - )"\-
15/0
9- /s^l
HRAKER It
/9-S*af
77.9^^2.
-77. 97^59
77. ^7 ^^
77, 97 6 9
77, 9t^^
o . o ^9^
CALIBRATION WT
WT AMOUNT =
PRE WT
^5, 606O
W.IWf
5 O . OC& /
POST WT
<,£> . OCfj ~L^
V7.999V
SO ' Ot><3 /
ROOM CONDITIONS
RELATIVE
HUMIDITY
VY®6 7.
V4>Cf
?<&>-)(
BAROMTRC
PRESSURE
Zf-95
't-?
T-9-9-Z1
Initials
0<<4.
y*cj£
fa <•#
en
i
n
o
Ul
I
—i
i
00
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A+E+C) =
_rng.
-------
.CLIENT E Pft
PARTICIPATE WEIGHTS SUMMARY ' Page.
RUN No. CC<~-9£-/V? Placed in Dessicator: ]
of.
ES PROJECT &D
STOVE MODEL No. CC /
POSTEST
Acetone Lot 0.
Acetone Sample Volume.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE/TIME
\0 - it
lo-l'
>fo ^
/ 5 /^
•
c,./S-S9
RKAKER U
/2-' 0&&O
Lfcj ^ > 000 /
ROOM CONDITIONS
RELATIVE
HUMIDITY
W®&-)'
4/1 ®k0
^®7/
BAROMTRC
PRESSURE
•z7 C/?
I
^c^
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
o-o
o
O , 00
TOTAL PARTICIPATE CATCH (A+B+C) - 5/3.0
rng
-------
CLIENT _h___
ES PROJECT r\D
PARTICULATE WEIGHTS SUMMARY Page of
•
RUN No. CC^- <~>G--~}4 Placed in Dessicator: Date/Time A>-/o
STOVE MODEL N
POSTEST
WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/£-//
lfs/f>
lo -'I
><=> ^
JO-IT- *v
Il~)0
}&- 1-^L,
>syo
9-/7-S °l
FRONT
PTF.TRR It
/}£-<*/
L/V13
^
/. nqt-
i.n 1
^x?m
. 6 W<£
>^17o
0 ,013-?^
CALIBRATION WT.
WT AMOUNT -
PRE WT
, 5^£>
- ^ S,f) /
• ^OOCJ
„ ^&oo
POST WT
, 99^
. ^7/
, ^O/
. V99^
ROOM CONDITIONS
RELATIVE
HUMIDITY
V
n^>?
n
i
n
Ln
I
I
t '
o
(A) (B)
u,cA
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT
ES PROJECT AD
RUN No. CCS-. 3^^7
^^?. -???o7
Srt. ?^^7
<2o. ^7?o
^3 o^37
CALIBRATION WT
WT AMOUNT -
PRE WT
*5 <* . <3 oao
4?.
**<=./>
s*?4
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
TOTAL PARTICULATE CATCH (A+B+C)
jne-
-------
CLIENT .
ES PROJECT f(D
PARTICIPATE WEIGHTS SUMMARY Page of
i
RUN No.CC^-^^-^/S Placed in Dessicator: Date/Time (p-fe^' ot>
7V
NT 3
\,
WT 4
lo -
FINAL WT
TARE WT
-------
Client
Date
WOOD HEATER CERTIFICATION TEST INFORMATION
EPA- Run I -CC5-7
ES Project }
\ "2- "b
Wood Heater Model
Operators I/O ^ if
TEST RUN INFORMATION
Attempted Burn Rate (£g/>w)
Achieved Burn Rate (Kg/nr) '
Primary Air Setting
Secondary Air Setting A/6
Thermostat Setting A/A
Other Settings
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (J)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
?.~ Z**^— Comments
Veloci ty Traverse
Temp
A i
2
3
88
§8
Ave.
Pitot Leak Check
Static
G-CC5-7-13
-------
o
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client /TA/l _ Run 8
- /
Date }0~<3--cbf) Uood Heater Model CC
ES Project 8 flf) /23 Operators /k^
Test Fuel Charge
Coal Oed Z-:
Page / of 3
Time
SampH ng/
lock
5T
'T
// /r
/ 55"
Test
:uel
Wt.
(Ibs)
10,
•3.8
10 .
"7
a.
•7.7-
,ue
Draft
(in
Comments
-'1,6^1
-dJ^lS 0
Combust or Temp.
lot?
887
-75'
fV C;
Top
-if,1!
V6/
Rear
Surface Temp.
'/HI
bottom
6-3
TFT
3d 7
327
37,3
-!££L
3 5o
Ilight
212.
eft
231
J202.
Stack
Temp „
r/' 7
?to /
•V7?
V/v
'31?
oil .
Tun.
Temp .
//v
77"
_27_
Til
-7-7
7ft
Room.
Temp .
2^.
72
7 3
70
•7U
7
-------
ENGINEERING-SCIENCE, INC.
Date
ES Project f
WOOD IIEATEIl CERTIFICATION TEST
TEMPEUATUIIE AND FUEL CONSUMPTION OATA SHEET
Run H Q^ -7 Test Fuel Charge
Wood Heater Model tX-!5O Coal Bed
_ Page ~
Operators
>
o
i
o
n
Ln
Time
Sampling/
Clock
i-zss
5"
IbIS
Test
ruel
Wt.
(Ibs)
•2*^
•Z
•o
Or/
Fl.ue
Draft
(In
?0)
0,0 '3
0.0,35
O/o '3
,c .^-fo
0,
Comments
-//o / *T -mac
Combustor Temp.
779
57 /
538'
i.
*?>79
.£_
7
fro/
I^L
W3
•2,75
•?>$/
32"?
•32-7
Surface Teiop.
Top Ijear Bottom Uight Left
7,07
373
159
3V Sf
-B
309
-1/0_
3^7
3« 9
3/5L
32. v
c 'c."6
337
33o
3/F
323
3/X
3.23
Stack
Temp .
2^2.
v/v
•57S-
223.
._y£
7,? 2,
Oil.
Tun.
Temp,
77
71?
2i
^L
70
7V
33
77
Z2.
77
7V
77
Room.
Temp,
7
•76
~70
75"
7.5"
:2£_
76
70
70
70
7/
-------
ENGINEERING-SCIENCE, INC.
CUunt EPA Run H
Date
ES Project f ft fl
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Page
of
Wood Heater Model
Operators /'-/ eft f(J //
/
o
i
o
o
VJ1
I
«-4
I
>—•
O
Time
ampling/
lock
Hi 5
Test
Fuel
fe.fi
z.o
/.o.
l.ue
Draft
(In
65 -V
iQSy
037
,0-35
Comments
Tfrf-
Combust or Temp.
/O L 7_ .
fop
771
V/J
Y/S
176
Surface Temp.
Rearl Uottoni |Right| Left
76 J
V31
73 y
3-3?
383
•2-87
7.T7
7
^f(
•386
Stack
Temp.
31-7
577
37^.
Dil .
Tun.
Temp.
32.
7?
•70
#7
&<-/
Room.
Temp,
1 I
7O
7o
7
7?
73
72
77
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CC.1^
Date
Samp
Samp
Run
Oper
Ambi
Bare
Stat
Filt
Mete
ding Locat
le Type
ion X^v^1 1
Start Time /6~^^ j\
Stop Time ' N
Probe Length and
Type . jz1/ .r^«-_S
KSo- Pi tot Tube Coefficient , ?'? "
Number V. v\.
ent Temper
imetric Pre
1c Pressur
er Number!
r 6
ature
isSure
e, (P 't
Read and Record All Data Every /O Minutes ' ^)
o
i
o
o
en
1
1
t— '
•^i
Clock Time
Sampling (24-hr
tlme.min Clock)
O fc>?,s
/o /a IS
?o /o <;T
*/o //o^
5o // / *5
bc> // 2 ^
77.f9
17.0 I~1?C
f^O X2. ?o /3<*5"
/7 iHi^
•V.V0 /VZ<^
Gas Meter
Reading.
(vm) ft3.
36>&* o
372.. S
/^•sz. *7
38 7. 6
3^7, v
^ '2. 3
^/S
.03?
• o "?^
.0 35
. o~?*->
.O"5S
.o"^S ^~>
i^^fs
,07) S
. <^"35>
10"? "S
.0-3,5
x°3 S
.0-3^,
• "^'b
•°'?)5
^o-^S
.O-TJ^
«>^> ^ 5"
•> o *^<^
0 ,^1-3 S
'ressure
;ntial
HZ0
Actual
• CiS
• 8>^
« 5 S
. ^s
'S'S
vVc,
.^s
• Sf's
, y<~^
.'6^
I "J5S
, Tr^
, 'JJ'1;)
> #S
• ^S
1*8^1
r S3
<> 8^
. 9. ci
<• 5^
f?3
S3
??^
•"j? 3
0 z
^Z.
7^3
Z'i
^ (/
%&
8 7
95 7
g
~?o
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7Z-
7?)
7<
76
77
-7.0
'0
7V
7#
~Ttf
7%
•7*7
~7%
Y7
7-7
%<^
'Rf?
X /
_% -z.
S "2.
•85
Filter
^f
Impinger
5 3
<3
7Z 5"o
7 73 ^>/
'7V •>'/
7V 57
7 y -=,- /
71/ f>'/
7?,
57
7 3 6" /
7-7-
t7 « —
73 ^T2_
7^ "51-/
77
77
5 £
5"y
7 S^ 5 y
^^r 5" i/
7 9 5" 5"
, 13 $*?
Pump
Vacuum
in. Hg
z_
•^_
•p
-z.
-2_
-^
2-
Z-
2_
"t-.
2_
^
>
"2_
Z_
7_
"2^.
p"
~£_^
"2_
?
Flue Draft
in. H90
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Hood Heater 7
15
83
7?
73
8
z
7?
7 3
/(,
•TZZ,
,035"
o 3 5
75-
7V
5V
_^SL
-TV
53 7.
• 0-3 S
7?
no*
,•6-5
71
7V
511.-J
7?
J.
57
o
I
o
o
Ol
I
-J
I
t—•
OO
56 Z.
S7Z.
V-
ss-
-------
S.-SE3
A-am
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Wood Heater
Date
CC-S
Sampling Locabion
Sample Type
Run Number
Operator l
Kcfx
^\Clock Time
Sampling\(24-hr
time, min\Qlock)
• — ' •
V&o l&z<5
tno /&3 -5
5oe> ,"& v1^
S/o /#S"S
S^ /^S
5'30 /«)/«=,
5VO U^S
55'0 /I 3 5
5^0 <"7V^
54 «
Gas Meter
}eadi nq
(VJ ft3
5^Z- ?
587,^
592^
&-1, ^
^2.._3
(eol^
£/Z.*7
fo/8.0
6^3.o& I
777.o«
Veloci ty
Head
UPS) in.
H?0
,0'^.cb
/c.3S
>o'3S
•^ -3S*
.o~\, S
,0-3 3
• .03-^
^5S
.^•35
. ^ 3<;
Ori fice Pressure
Difrerential
(All), -in. H?0
Des.i red
. V®
. ^s
'?iS
."rSi
• *S
' .^3
^S
,c^S
,^S
Actual
>%©
^!S
-•8-5>
•8S
.»S
-crfS
.^-.s
• «S
.3-5
r *5
TEMPERATURES
Di lution
Tunnel
],
,
*lf0S
Meter
In
S9 •
^'7
iy;
9^
8r;
^7
^7
Hfc
»^
\
^/
-
Meter
Out
S^V
»V
-^V
8S
^S
^V
?v
8V
^
/
/
7
r
Filter
82
W
a/
»/
so
%
tfo
7V
7V
Impinge'r
^-7
60
&(j
&/
&/ .'
(0-2-
&-Z.
• 63
£3
•
Pump
Vacuum
in. Hg
^
"*_
il_
d
2_
2.
2_
<^_
~^_
Flue Draft
in. H?0
1
L.
!
1
i
I
o
o
-------
ENGINEERING-SCIENCE, INC.
Wood Heater cc-5
Date /A-9-P.-e?
SAMPLING DATA
Sampling Location
Sample Type
Run Number_
Operator
Start Time_
Stop Time
- 6G- -
Ambient Temperature
Barometric Pressure
Static Pressure, (P
Filter Number(s)
Meter
Probe Length and Type_
Pi tot Tube CoefficienT
Assumed Moisture
Sample Box Number
Meter Box Number /
Meter H
Pretest Leak Rate
Post Test Leak Rate"
1 1'1
oo
-3-7
Read and Record All Data Every /O Minutes
Clock Time
(24-hr
Clock)
Velocity
Head
H20
Sampli ng
time.min
Gas Meter
Readi ng
Ori fice Pressure
Differential
( H), in. H?0
Desi red
Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter
Impinger
Pump
Vacuum
in. Hg
Flue
in,
Draft
H20
0
/to
/«
/o
035
¥3-
7.0
/o
^35
.90
77
//of
7?
73
7
-------
SAMPLING DATA (cont.)
Vlood Heater CC -
tNUINfctHING-SCIENCE, INC.
Date ./£> - 9 - 8*7
Sampli
Sample
ng Location /^5-^S- -<^? ^
Type ^
9^ / *7
Z6*> ft/*-/1!
•2-7,0 /'/T<
"Z^o /S/2 5
"3/o /5"3
3^x3 //'i"5"5"
3^0 /4>t>r"O 1(0*45
•39(t~>
Gas Hater
Reading
(V ) ft3
V5&7.J?
V 7^ <^ T *)
-. "7 £~
* 0"*J ^
. — z '5
•A o ~*> *5
i 0-35
oo 3 5^
* o 3 5
• °"i S
.^ "3.S
. 0-3 <;
'£'3<>
,0"3,S
,^>35
, 03S
,•=.-3,5,
i^^S
.<^1>S
Orifice Pressure
Di f ferential
(AH), -in. H?0
Desi red
Actual
/
^ ^<-,
* C1 0
« ^/^
- 9 &
.9e>
e c( O
f 9o
,. 9o
• 7c,
.1 £>
t9o
/?o
^O
^o
.90
, c/o
.9^
; ^ ^
.50
TEMPERATURES
Di lution
Tunnel
Meter
In
ft"?;
?) ^7
157
^V
^ "^
3 ^
ST.
ft "21
"S Z
S 3
% Z
87,
c?^-
g"3
§ 7).
Sfy
%,.
D7
e'S
Jl
^7
Meter
Out
^ S
!j S"
35
^,Y
r -^
O j
?5/
"8^
>oo
79
So
??
77
•7';
77
7^
^o
^l
(5 i-
tJ 0)
rtfH
yL/
Filter
79
79
7 */
7?
7V
73
7"Z
7/
7Z
7-Z.
7 3
7Z-
TL,
1 '?>
7 V
75
7ft
O ^
%
o(
^/
Impinge'r
5
^-^
5"f>
f>°/
£>" *?
frO
60
-------
£:.irn
tfiEEQ
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater
Date
CCS
IL> -°t - 9 c\
Sampling Location
Sample Type
Run Number_
Operator
IZDEE
CCS- TV
\. Clock time
Samp11ng\(24-nr
time, min\Clock)
~ " " ~— — - — — ~_
V'P.O 1 & 2-*^
*1*0 /935
5'eo /&
Gas Hater
Readi nq
(V ) ft3
5K2. ?<
5^-7,^
5r/^¥
51? 7, ^
60 2. ^
60 7<7
GfL.'*!
(e(8 .&
CeZ^.ofrL
r7 0
>c/0
Actual
,9o
.^0
,?o
,'?C'
,c(0
>ciD
,c/o
.
yo
^7
7^^
€^
•»%--
\
«a
-'
Meter
Out
<&>
^
c%
^
^
X6
«s
es
8S
/
/
.^
Filter
^1
B|
*6
•S-6
"fc
&
r?
71
7^7
Impi nger
<-(
t^(
•
Pump
Vacuum
in. Hg
-^
~^
7_
-ii
^
->
2_
2.
i_
Flue Draft
in. H?0
o
I
o
o
I
to
to
-------
FUEL MEASUREMENTS
Date
Project No.
Run No. rtf
Wood Heater Manufacturer
Woocf Heater Model
.. —j
Circle One:
Fuel Type and Amoun
Ideal Load Weight
Fuel Piece Length
Moisture Meter Calibration 12T
v)voi p. °F
Actual Load Weight
Piece No.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Moisture Content-(Meter - Dry Basis)- Co»vK7t
-------
FUEL MEASUREMENTS
Date
Project Mb.
Hood Heater Manufacturer
Woo
-------
TEST
CC5-8
WS\RD123.40
WM1381A.APP
-------
Method 56 Proportionality Rate, Flou Rate,
Burn Rate, and Sample Volume Calculations
Stv manu: ORVILLE
Model no: CC150
Lab name: E5
Tst date: 10-10-89
Run no : CC5-5G-8fl
Tst time
(min): 528.00
Chrg ut
(Ib uet): 39.30
run
time
(min)
0
60
120
180
240
300
360
420
480
528
vel dp
(mm H20)
(m.H20)
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
Units 1-metric,
2=English:
Y, DGM:
Pi tot co:
Gas MM :
Pb (mm, in. Hg):
Stack area (m2,ft2):
Wood moist (.'/. uet):
Burn
stack
temp
(C,F)
95
102
100
99
112
102
121
105
118
108
DGM
rdg
(m3,
624.
654.
685.
715.
745.
775.
806.
836.
866.
889.
ft3)
522
700
000
400
600
800
000
000
000
963
DGM
temp
(C,F)
73
78
83
86
88
89
89
87
86
85
Samp vol
2 (sm3,scf)
0.995 256.686
0.99
28.56 Flou rate
29.92 (dsm3m,dscfm)
0.1963 . 137.77
17.23
rate (dry kg/hr): 1.68
DGM dH
(mm
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
H20)
880
880
880
880
880
880
880
880
880
880
vel
(m/min)
(ft/min)
776.50
781.38
779.99
779.29
788.30
781.38
794.48
783.46
792.42
785.54
PR
(Z)
102.4
100.9
100.3
101.5
98.2
102.2
97.1
101.1
98.3
dDGM
vol std
(m3,ft3)
29.798
29.640
29.464
29.110
29.003
28.950
28.759
28.864
23.098
85.49
17.640
460.00
1850.00
vs/VmTs
0.01
vs ave stack
ave temp
(C,F)
784.27 106.20
o
I
o
n
01
I
oo
I
-------
Jfethod 56 Proportionality Rate, Flou Rate,
Burn Rate, and Samp19 Volume Calculations
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
528
ORVILLE
CC150
ES
10-10-89
CC5-5G-8B
528.00
39.30.
vel dp
(mm H20)
(in.H20)
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
0.036
Units l^metric,
2=English:
Y9 DGM:
Pitot co:
Gas MM :
Pb (mm, in* Hg):
Stack area (m2,ft2):
Wood moist (.?. uet):
Burn
stack
temp
(C,F)
95
102
100
99
112
102
121
105
118
108
DGM
rdg
(m3,ft3)
624.522
654.700
685.000
715.400
745.600
775.800
806.000
836.000
866.000
889.957
DGM
temp
(C,F)
73
77
83
87
88
89
89
87
86
85
Samp vol
2 (sm3,scf)
1.009 260.294
0.99
28.56 Flou rate
29.92 (dsm3m,dscfm)
0.1963 137.77
17.23
rate (dry kg/hr): 1.68
DGM dH
(mm H20)
(in.H20)
0.880
0.880
0.880
0.880
0.880
0.880
0.880
0.880
0.880
0.880
vel
(m/min)
(ft/min)
776.50
781.38
779.99
779.29
788.30
781.38
794.48
783.46
792.42
785.54
PR
(?i)
102.
101.
100.
101.
98.
102.
97.
10L
98.
4
1
3
3
2
2
1
1
3
85.49
17.640
460.00
1850.00
dDGM
vol
(m3,
30.
30.
29.
29.
29.
29.
29.
29.
23.
std vs/VmTs
ft3)
217 0.01
113
879
465
411
358
163
270
417
vs ave stack
ave temp
(C,F)
784.27 106.20
o
n
o
Ol
t
00
i
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
DATE DEPLOYED )o-fo -
DATE RETRIEVED
TEST LOCATION^
TOTAL (MG)
SAMPLER SN# 9 6> 2- Z. "7
(HG BAROMETER UNCORRECTED)
PRETEST B.P3o.<3f (IN HG)
'TANK 1^,95 (--IN HG) TEMP, ^i-(c)
TORR ABSOLUTE Z . 3
POSTTEST B.P. 3o.g/ (IN HG)
WEIGHT GAINS
PROBE — Z .
LINE
CONDENSATE
FILTER#1
FILTER*2
o .3
8."7
. 7-
-O. /
. ,_
S.Vo TANK / /, /£>
Tcr
TORR ABSOLUTE
_(—IN HG) TEMP. ~L-/
^^
(C)
PRETEST LEAK CHECK
TEST TIME £2 § (MIN.) g.
STOVE ID
WOOD SPECIES
WOOD MOISTURE (Z DRY) 20-9"Z-
WOOD MOISTURE (Z WET) /7< ^^
WOOD CONSUMED (LB) "3^,3 (KG)
SAMPLE FLOW RATE PRETEST
ROT3HETER ^> %^ •= (ML MIN) 60
POSTTEST
ROTAMETER
= (ML MIN) $ *%
START
(IN H@0) FINAL
MIN.
zy.
DELTA
G-CC5-8-3
-------
ENGINEERING-SCIENCE, INC.
DATA SHEET VPI IN-SITU TEST METHOD
WEIGHT GAINS
K./5
DATE DEPLOYED lo -/& -.'I *? °\
DATE RETRIEVED
TEST LOCATION^fS - U) S - L&k
SAMPLER SN# ^ (j, 1 T, C f
(HG BAROMETER UNCORRECTED)
PRETEST B.Plo.oV (IN HG)
1ANK. c-//1-/ ^> (. — 11s n(j) TF.HP .
TORR ABSOLUTE "Z_ . 3
POSTTEST B.P. 3£>, tf / (IN HG)
PROBE — Z. . /
LINE o.-?
CONDENSATE 7 . £
FILTER* 1 £, O
FILTER//2 ~ O . ^
TOTAL (MG) / Z . 7
T-1.(C)
TANK /7, /£" (—IN HG) TEMP. "Z_/ (C)
TORR ABSOLUTE ^~2L(c> . £>
PRETEST LEAK CHECK
START (0 . 1 (IN HQO) FINAL «^ ,(-
2_(IN H20) LEAK RATE
RUN# CC$~ I/ 'PL ~ ^ /^
Ifcb I I ilrt > fc " ^WiN . J » • u
STOVE ID cr - /*T<9
WOOD SPECIES O&u^ /A?<; A^
; "c
WOOD MOISTURE (% DRY) Z^-bl.
WOOD MOlolUKE (,/i WET; 1 i. *. ->
WOOD CONSUMED (LB) 31. b (KG)/7.S
SAMPLE FLOW RATE PRETEST
"RnTffltfTT'FP /C* *5T^ — fMT MTTJ^ /^/*^
POSTTEST
ROTAMETER d I =(ML MIN) ? f
<£>/ "2- (IN H20 MIN)
POSTTEST LEAK _CHECK
START S'~) (IN H20) FINAL 5\ g" (IN H2) LEAK RATE O.
(IN H20 MIN)
POSTTEST GAS ANALYSIS
RUN COMMENTS:
//.
GRAMS MASS AFTER FLOWING 0.5 1pm NITROGEN FOR INDICATED TIME
PRETEST +_£/£/ MIN.
MIN.
MIN. + MIN.
DELTA
PROBE+FITTING 3V. g 72V
SAMPLE LINE
CONNECTOR
3V,
G-CC5-8-4
-------
PART1CULATE WEIGHTS SUMMARY
Page.
of.
CLIENT t.
ES PROJECT f(D /23
RUN No.
in Dessicator: Date/Time/^-//
STOVE MODEL No. CC -/
POSTEST
' WT 1
WT 2
WT 3
WT .4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
I&-1/
/6 10
lo - /t-
'/T.^-5
•
Cf^/y-yc)
'
FRONT
FTF.TKR If
Stt-^q
« /T-7/
• /Z")?_
. 1111-
•t fL/o
O.ao62,
BACK
FTLTRR It
^/" -7^7
« I1-o$
* /Zo<£
« /7_o«
. /ZO*)
"0, ^<3<5/
CALIBRATION WT.
WT AMOUNT =
PRE. WT
« O
ROOM CONDITIONS
RELATIVE
HUMIDITY
v^7y
V* ^7/
BAROMTRC
PRESSURE
•2.9. 8 S
"5^?, C^t'O
Initials
i
y^C^>
/nc<
o
I
o
n
Ui
c»
I
UI
(A)
(B)
-------
CLIENT
PARTICIPATE WEIGHTS SUMMARY Page of
RUN No.CC, 00 <3'7
CALIBRATION WT
WT AMOUNT -
PRE WT
So ,cto/
-------
PARTICULAR'S WEIGHTS SUMMARY
Page.
of.
CLIENT
ifP/9
ES PROJECT Rf) II 3
RUN No. CC 5 -OPI-%& Placed in Dess icator: Date/Time
STOVE MODEL No. CC.
POSTEST
1 WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
lo - //
/6>~*,o
)v - 11^
/T, 1 ^
9_/7_3^
'
FRONT
PTF.TRR It
**£--) f
. / -Z.-M
. I1SW
• /I?-/
„ /Z/V
o<# ^o <6-o T5>
POST WT
» 5"^>/
» ^en,®
ROOM CONDITIONS
RELATIVE
HUMIDITY
W®?¥
Vo&W
BAROMTRC
PRESSURE
z^f jr^r
Je> ,.&<=>
Initials
t
/^i <=*,
^^/?
\
I
o
o
-------
PARTICULATE WEIGHTS SUMMARY
Pa ye.
of.
CLIENT
RUN
in Dessicator: Date/Time /^ ~'l
ES PROJECT R D X2
STOVE MODEL No.
POSTEST
Acetone Lot II 9 // V
Acetone Sample Volume / O
'.
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
TARE WT
NET
DATE /TIME
lo- ii~
l^oo
lo - /i-
/<* 1^
•
^wb-w
BRAKER U
/)-7o
77. SSZo
7?. 5S-/S
71, S
CALIBRATION WT
WT AMOUNT -
PRE WT
5^ , &t& 1
So . Croof)
POST WT
5<3/ <^>^ /
V<7.9999
ROOM CONDITIONS
RELATIVE
HUMIDITY
V^7*"
05^7^
BAROMTRC
PRESSURE
-7 *?,9TL-
-2.9^?
Initials
/^ c/r
^'c^
T "
O
I
O
O
Cn
I
CO
CO
(BLANK CONG.) x
(ACETONE SAMPLE)
WT GAINED
o
TOTAL PARTICULATE CATCH (A+B+G) =.
_mg.
-------
CLIENT
ES
PARTICIPATE WEIGHTS SUMMARY
Page.
.of.
RUN
Placed in Dessicator: fiat. P. /Time
- /A-- /7/
/Z3 STOVE MODEL No. CC
POSTEST
Acetone Lot It
Acetone Sample Volume
WT 1
WT 2 .
WT 3
WT 4 •
WT 5
FINAL WT
r
TARE WT
NET
DATE /TIME
10- / 1*
I^HO
to - i~L.
l*o*>
•
q -/$-«&e,0t>o(
^9,999^
ROOM CONDITIONS
RELATIVE
HUMIDITY
VO&7-L-
Y6^ 70
BAROMTRC
PRESSURE
~*>o. &&
^9,%*}
Initials
sx c#
K^t
o
n
o
Ui
I
(X
I
vfi
(BLANK GONG.) x
(ACETONE SAMPLE)
WT GAINED
O
O.
(C)
TOTAL PARTICULATE CATCH (A+B+C) =.
/ 7° • °
rng.
-------
PARTICULATE WEIGHTS SUMMARY
Page.
of.
CLIENT _±
ES PROJECT kn /7
RUN No.rC9-$&-%/? Placed in Dessicator: Date/Tims /o-//
STOVE MODEL No. C_f_
POSTEST
Q
' WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE/TIME
le> - I/
itz*;^
10 - /T-
/-t,/ 5"
la - /t-
;sv^
<7-/7>2f<5'
FRONT
FTF.TKR I!
AT-6«?
6
..^^^.7
^1Z7
^67^^
d./?V3
BACK
Flf.TRR It
^"-/^6
£7
.^tfW
/^•?^^
* ^^
< 5\j V5
~*>G>, C^5
•z.9.9^
Initials
a
>*i^^
^l^C^
*c£
o
o
o
01
»
00
I
(A)
(B)
-------
.CLIENT
PARTICIPATE WEIGHTS SUMMARY
RUN No. CC5"- $6 -*&£ Placed in Dessicator:
of.
ES PROJECT /?/) t?-
STOVE MODEL Ho. r"C
POSTEST
Acetone Lot )l 9//
-------
PARTICIPATE WEIGHTS SUMMARY
Page.
of
CLIENT J|
ES PROJECT %D 12. 3
RUN No. CCS-56--% ft Placed in Dessicator: Date/Time
STOVE MODEL Uo.CC /
POSTEST
•'
WT 1
WT 2
WT 3
WT 4
FINAL WT
TARE WT
WT GAINED
DATE /TIME
/ o~ //
/5SS
lo ~ fL. ^K-
/T. / ^
jo , /-(-
1 <> V S
'
9-/7^7
FRONT
PTF-TRR II
/5^r-6 ->
.%3So
.tiM**
,K32/
.**!<*
«67<^
0.1 56Y
BACK
FTF.TRR II
/*£"-£<*
.6 -5? T7
.£,
0,oo^
CALIBRATION WT.
WT AMOUNT =
PRE WT
. ^000
> *:>£>& 7o
BAROMTRC
PRESSURE
13, 1$
3?O .
-------
WOOD HEATER CERTIFICATION TEST INFORMATION
Client ' Rfi/l Run /
Date Id -lO ~
ES Project
Wood Heater Model
Operators U)
/SO
TEST RUN INFORMATION
Attempted Burn Rate flCgX-hf1) Cj/V Secondary Air Setting
Achieved Burn Rate (Kg/hr) IjGT"? Thermostat Setting
Primary Air Setting rux)c Other Settings
c*
FACILITY CONDITIONS
Barometric Pressure (in Hg)
Room Temp. (°F)
Relative Humidity (t)
Room Velocity (ft/min)
Scale Audit
Surface Temp. Ave. (°F)
Cold Draft
Pretest
-73"
Post Test
2,^-85 •
S*/
TEST FUEL DATA
Firebox Volume (ft-) _
Fuel Charge Range Wt.
Actual Fuel Charge Wt.
to ||.-7
Coal Bed Range Wt. "Z.l to
Actual Coal Bed Wt. ^ Z.S
Fuel H20% Dry Z^'-
Fuel: Dry Kg
Wet
Hi
LOADING/TEST START OPERATIONS
By-pass C
DOOr QjOu-r\
Veloci ty Traverse
Air Settings
Comments
Temp
A 1
2
3
_ B !
Ul 2
"I ID 3
4 Oi630 Y*\ 4
Ave.
Hi
Ul
Pitot Leak Check
Static
G-CC5-8-13
-------
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
ENGINEERING-SCIENCE, INC.
Client ^f\ ' Run I
Date
ES Project f
*T> - 8
Test Fuel Charge
Page
of 3
Vlood Heater Model
Operators
tc;o Coal Ded
o
I
o
o
Ul
oo
I
line
ampling/
lock
//Q5
_SL
// -? 5"
est
uel
•/t.
Ibs)
Fl,ue
Draft
In
7.6
M.S
3o&-
.070
,050
C7Z
.060
Comments
l\V -
Combustor Temp.
' \ '-i
3*0
I fid
"7VZ
7Q7.
//5V
j la <7
'
6pJ_.
^8_
399
697
5^7
IJottom
-^^SL
35V
lUght
'-/ / 7
W7
v?v
V57
TeTt
7 1
Sto?
55V
39 y
5V
Stack
Temp.
HZ.
6/9
Oil .
Tun .
Temp .
>**+
//o
Room.
Temp .
76
75
25_
75
75
77
23_
^2_
77
77
7V
-------
ENGINEERING-SCIENCE, INC.
Client £ P/) Run Jf
Date
ES Project f /{ p
WOOD HEATER CERTIFICATION TEST
TEMPEUATUIIE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Coal Bed
Wood Heater Model CC -/
3
Operators /Mc/( Id
o
I
n
o
t_n
I
oo
I
Time
Sampling/
Clock
Test
:uel
Ht.
Uki)
/*//<;
S
A/55
'735
'7-5-5
5.7
Qj-L
:l,ue
Draft
(in
ML
^;.v 5
cObl
i cfao
uj£
£>1(f>
.0-7 ZJ
Comments
/V26
dctn
L^ '3
Combustor Temp,
•74-3-
73
-7/3
7V/
//59
77.
7?^
78
72-S
lop
%
//
»
Surface Temp.
Hear
5/v
fz^Z
39 f
1T5V
Bottom
"357
35
3V/
l6t
Uight
537
53V
2/2_
Left
^2/_
V77
V97
5V/
^5^
V7Z,
931
Stack
Temp.
5V S
753
670
<^^
SV/
S5/
^rLZ.
Oil .
Tun.
Temp
9?
52.
//a
/tf?
ill
1/7
Room.
Temp.
7JZ.
Z?_
STL
s-/
2LL.
s/
8V
c9/
-------
ENGINEERING-SCIENCE, INC.
CHunt £TPA Run i
Date
ES Project J
WOOD HEATER CERTIFICATION TEST
TEMPERATURE AND FUEL CONSUMPTION DATA SHEET
Test Fuel Charge
Wood Heater Model CC/5Q coal Ded
Operators
Page 3 of
o
I
o
o
00
I
Time
Sampling/
lock
/8V5
/8
/<=>
^35
Test
Fuel
It.
(Ibs)
Z.8
1,5
U<=>
o,
3
i
, 5
0,o
l.ue
Draft
(In
IpO)
072.
0.7 "5
'075
,'OCeO
Comments
o.o ,
Combustor Temp
IQ<> ^
TTB
876
Ail
537
5V iL
Top
7/1
Rear
Surface Temp.
bin
5"ciO
-51 "I
ML
51?
573
Uottom
37^
Right
532
5V V
SV7L.
533
JZ5L
Left
5V5
5V
50?
5-5
2JLL
Stack
Temp.
236.
Oil .
Tun.
Temp,
ni
/o?
'03
7F3-
/ZXJ
77?:
tto
Room.
Temp .
82
&/
S3
*L
-------
(yii2&*bj u*«-«*'^pj
•31-ysa.pj tjj-'-'^.i-jS*
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater OCfJ
Date
Samp
Samp
Run
Oper
Amb1
Bare
Stat
Filt
Mete
! /•& -/O - £i "y
i ling Locat
»le Type
1on fc^T"^ /
Start Time I I ^ -> ./-
Stop Time
Probe Length and Type ./^i '' G /st c(cfLi~J
Assumed Moisture c/ ^o
Sample Box Number X^
Meter Box
Meter H
Number /j;^ 7Pr ^, /^
Pretest Leak Rate .dot,- ^ /
Post Test
Leak Rate .e^W S- 6
, /
Read and Record All Data Every /O Minutes
i
0
o
1
oo
1
H- '
-J
Clock Time
Sampling (24-hr
t1me,m1n Clock)
0 IMS
Z<=> JT.O^
1° till
L/2$
I/O /"? 3T
l%£) y^VCJ
)T,O t -^ <~-c;
/ tVtt
no /V3c
l*n /VV5~
/ ^7/5 / ^^ ^j ^"
2 ^£^ / ^^& ^t
"i/o /5X"
"2? /<~7£-
-2,-r>, /$-5
So "3 V> '7
^^9*^Z
^vv» *7
^y?» "7
<^^v,. -7
fa6>V» ^
tofac) 0 ^
•^, 7 S, 0
6^0, ^
/ O1 ^^ ^*i
^9^" * /
(jff^ „ /
7/*J £) D *7 -^»
7<5« 3
7/0,, "^
7/5". V
7z^~ 'y
7^o 5^
•9^5* S
^'-/o t 5"
775. £>
Velocity
Head
( Ps). in-
H?o
• °3 93
,03 (c?
t &~*> 6?
e S> %#>
« <9 "^/^
e 6> "^ 6
„ ^ -2^ A.
t O ~?, O
„ -^ x,
* 0 "3 G
.tf t» '3<>
, C> -2, ^
e O "3 £
e O ~5 tf5
, ~*> & '
e O ~*> £
« 0 *5 C-
o "S <»
f£> 3 6>
flo3<^
On fice Pressure
Differential
( H), in. H?0
Desired
. o O
i c5 o
& f~) ^3
f rj (^
c K'ft
Actual
.*j®
' S^
u «,<&
f y K
* ftft
a 5.9T
. s «-
- x 9S
* "3 1T
* S 9'
/ ^^
« '^'S'
^ S
K i
'% 1
S7,
<% /
•^1,
sv
"?5<>
^-7
q- 7
S' *7
"^^
% c>
^ 7
*» 7
1S"7
...fy^-
Filter Impinger
7^ "?y
7? 5 2-
SS 'VT
^y 5"y
% z 5y
S/ 5y
^7. 5*5"
<^y ty <^
8T V7
^ "5" V5^
^ 5" -V7
85" y &
S5" V<^
ft*5 S/
*£ S-71.
"51 "S" S ?;_
c5 *X 6" 7 _
^ >i 52_
Pump
Vacuum
in. Hg
~2_
^.
*2_
T-,
•7
•2_
•7^
~2_
^_
•7
'2_
-^
^
•z.
7.
7.
-^_
J2.
~^,
"Z_
'2_
v
-?
^
<2-
Flue Draft
in. H90
-------
33
21 {
SAMPLING DATA (cont.)
ENGINEERING-SCIENCE, INC.
Hood Heater c.C- ' ^°
Date //;> ~ /<^) "^
-------
SAMPLING DATA (conb.)
ENGINEERING-SQIENCE, INC.
Heater
fo -/
V/ood
Date
Sampling Location
Sample Type M
Run Number
Operator
cc-S
CCS -
- p,A
• "\^ Clock Time
Sampl1ng\(24-hr
time, min^x£lock)
• " — • — — —
t/RO m.5
ijqo /<2ss
$00 ^oo5
<$(0 •zoi'S
S'z-o ^o 2,5
SZ-S* ^°3 3.
ci^r
Gas Meter
Reading
(Vm) ft3
es^-o
B7Ao
fW-e
QB l.o
08o; i
88C/,'?6'S
Tf.5.W/
Velocity
Head
UPS) in.
H?0
(0-3 O,
^o^o
,03 te-
,^3G?
^O^Q
,03^.
.0^
,«^
TEMPERATURES
Di lution
Tunnel
/
V
Itf.-LZ
Meter
In
?o •
%
^^
8V
"Sf
88
^•7
-
Meter
Out
#£>
8.S
BS
#
V$
¥$>
Impinge'r
519
5V
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA
Wood Heater CCS
Date
Samp
/O'/'O-S0?
ling Location bT"^ /
Sample Type ^5^
Run
Number CCS - 5"6 - & &
Start Time ] I1-/ 3
Stop Time
Probe Length and
Pi tot Tube Coeffi
Assumed Moisture
Operator ovi^U ^ KcV\
Ambient Temperature
Barometric Pre
Static Pressur
F1 Her Number!
Meter f,o
!S5ure
e, (Pq)
s)
O©Q
Type . / ^/'v
ci ent , v 7'
i/
Sample Box Number /^
Meter Box Number M-Tkh ~&
Meter H
Pretest Leak Rate 0,600 (^ //'/
Post Test Leak Rate A^oti 0 /37I~
y/0 /3 3^
i?t> /?y$"
/3° I35^~
,Lj& / J^fl^i
£'& J^ /^
Zif ;/7 ^c^
^30 y <* ^?<"
ifo y^V5"
Gas Meter
}eadi ng
(vm) ft3
i) £. *7 , *3 ^_ *.
u?2- /*; ^^
^»"?y^7
(f~lCJr ?
ff) f^ff /
&lci« "7
fo'~»9 1 ~7
(^6-9* 7
ti/p'S t ^
{,->£> 9. TV
675- (7
£,<%<-)„
a n"hL->
* ci ~$ £•
« n"*)k
t o~3O
& & ~3>&
• u o3C"
tf f'"^^r>
- r» "5 £-
^^ 3 ^.
*{>'$£
e & 16?
,& 3 <2>
«^j -36-
* <9 "? ^'
,, rj •-*, /^
c O "•? f=-
• o "^ C»
, 0 ~*y (J-,
C^T) "^ ^?
Ori fice f
Differe
( H), in
Desired
.
% 3
9 <
?5/
^Z.
%s
^<^
S7
9:5?
^?
CLO
*-?'&
^2 o
^ O
9/
9/
9y
9-Z.
9" z_
Meter
Out
73
73
7 57
§'-g-
Filter
73
Impinger
7/
5" "2.
£/ 5 ^
8V
75/
5V
^ 1
79 S-?
79 5S-
^3 V7
§• "^ 'X7
» '? V 7
& 3
?) 3
vs-
ti/ ~3 S^ S^
r;-- • > ^y c^
% y v 7
5y ^^o
%6 So
^ S^ 5"c^
% £ 5c~>
V6 Sy
?rcr, 5V
Pump
Vacuum
in. Hg
^_
^
7
-^_
"7^
~2_
7^
"2_
~^
7
1_
"Z_
•7^
~Z_
^_
Z.
rr_
~PL,
~i_
T
Z,
-7
"2^
"2_
Flue Draft
in. H20
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater CC -
Date /s.
Sampling Location^y -1^ <,
Sample Type
Run Number_
Operator
/?
/•>>
Clock Time
Sampling\(24-hr
time, min^x£lock)
Gas Hater
Reading
(v) ft
3-
Velocity
Head
(APS) in.
Orifice Pressure
3i f ferenti al
jesired Actual
TEMPERATURES
Di lution
Tunnel
Meter
In
Meter
Out
Filter| Impinge'r
Pump
Vacuum
in. Hg
Flue Draft
in. H?0
91.
9 3
ZTYs
/6/T
73
L 7
_2A
7 7
-------
ENGINEERING-SCIENCE, INC.
SAMPLING DATA (cont.)
Wood Heater_
Date
Sampling Location_
Sample Type fJ^
Run Number cc^
Operator i^O B i~
"x. Clock Time
Sampling\(24-hr
time, miriXQlock)
~ ' — "
Y
,0^0-
i03^
-o-^^
• 0-3 t
Ori rice Pressure
Di f ferential
(AH), -in. H?0
Uesi red
* ^^
• •J'-Z-
.72-
vS z_
,92-
' ,9 Z
Actual
,9 T_
.?z
-9z^
.? ^_
• 9z_
.9?
•71-
TEMPERATURES
Di 1 ut ion
Tunnel
1
I
V
lo~l>tT-
Meter
In
7o
&
,5-8-.
5~c)
•
Pump
Vacuum
1n. Hg
S
Ct>
£
&
£>
£>
Flue Draft
in. H?0
o
o
n
00
I
NJ
NJ
-------
FUEL MEASUREMENTS
Date g> -/£>-•• S*^ _ Wood Heater Manufacturer flffjl
Project No. Kbf2,"b» Wood0 Heater Model CC /<5 O
Run No.
Circle One: '_<_ _
Moisture Meter Calibration 12% / z__ 221. ~Z~ 2
°P AS - . -
Moisture Content- (Meter - Dry Basis)-c<"v'*c7"c
-------
FUEL MEASUREMENTS
Date
Project
Run No.
Wood Heater Manufacturer
Woocf Heater Model
CC
-P3,
Circle One: Pretest Fuel
Fuel Type and Amount 2x4
Ideal Load Weight ;
Fuel Piece Length
4x4
x4
__
" Actual Load WeTght
Moisture Meter Calibration 12%
°F
221
Overall Fuel Moisture Average
G-CC5-8-24
------- |