EPA-450/3-76-010
November 1975

                SOURCE SAMPLING
       RESIDENTIAL FIREPLACES
           FOR  EMISSION FACTOR
                     DEVELOPMENT
    U.S. ENVIRONMENTAL PROTECTION AGENCY
        Office of Air and Waste Management
      Office of Air Quality Planning and Standards
     Research Triangle Park, North Carolina 27711

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                                     EPA-450/3-76-010
          SOURCE SAMPLING
     RESIDENTIAL  FIREPLACES
                     FOR
EMISSION FACTOR DEVELOPMENT
                       by

              W.D. Snowden, D.A. Alguard,
             G.A. Swanson, andW.E. Stolberg

              Valentine , Fisher & Tomlinson
                 520 Lloyd Building
               Seattle, Washington 98101
                Contract No. 68-02-1992
            EPA Project Officer: Thomas Lahre
                   Prepared for

         U . S . ENVIRONMENTAL PROTECTION AGENCY
            Office of Air and Waste Management
          Office of Air Quality Planning and Standards
         Research Triangle Park, North Carolina 27711

                   November 1975

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This report is issued by the Environmental Protection Agency to report
technical data of interest to a limited number of readers.   Copies are available
free of charge to Federal employees, current contractors and grantees,
and nonprofit organizations  - as supplies permit - from the Air Pollution
Technical Information Center, Environmental Protection Agency, Research
Triangle Park, North Carolina 27711; or, for a fee, from the National Technical
Information Service, 5285 Port Royal Road, Springfield, Virginia 22161.
This report was furnished to the Environmental Protection Agency by Valentine,
Fisher & Tomlinson, Seattle, Washington 98101, in fulfillment of Contract No.
68-02-1992.  The contents of this report are reproduced herein as received
from Valentine, Fisher & Tomlinson.  The opinions,  findings, and conclusions
expressed are  those of the author and not necessarily those of the Environmental
Protection Agency. Mention of company or product names is not to be considered
as an endorsement by the Environmental Protection Agency.
                       Publication No. EPA-450/3-76-010
                                      11

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                           TABLE OF CONTENTS


SECTION        TITLE                                                   PAGE

  I            INTRODUCTION                                             j_

 II            SUMMARY                                                  1

III            DISCUSSION OF EMISSION FACTORS                           2-12

 IV            PROCEDURES                                              12 -  20
                 PARTICULATE SAMPLING, CLEAN UP AND ANALYSIS,
                 POM SAMPLING, REFERENCE PITOT, INTEGRATED GRAB
                 BAG GAS SAMPLING, PARTICLE SIZING, FUEL DENSITY
                 AND MOISTURE CONTENT, WOOD WEIGHING AND FIRE
                 STOKING, GAS ANALYSIS

  V            APPENDIX                                                21 -  172

               A.   SELECTION OF THE REPRESENTATIVE FIREPLACE          22 -  23
                    WITH STATISTICAL CALCULATIONS

               B.   TABULATION OF THE RATIO OF BACK HALF CATCH         24
                    TO FRONT HALF CATCH

               C.   THERMAL CONDUCTIVITY GAS CHROMATOGRAPHY, GRAPH     25

               D.   INFRARED SPECTROPHOTOMETRY, GRAPH                  26

               E.   POM QUANTIFICATION, TABLE                         27

               F.   ENERGY BALANCE, % EXCESS AIR, CALCULATIONS        28 - 36

               G.   PARTICLE SIZING, CALCULATIONS AND GRAPHS          37 _ 47

               H.   VELOCITY CORRECTION COEFFICIENT, CALCULATIONS     43 - 50

               I.   WOOD BURNING RATES, TABULATION                    51

               J.   AUXILIARY ATMOSPHERIC EMISSION DATA               52

               K.   COMPUTER PRINT-OUTS OF PARTICULATE EMISSION       53 _ 81
                    DATA WITH CALCULATIONS AND TERMINOLOGY

               L.   FIELD DATA SHEETS                                 82 - 172

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                            LIST OF TABLES


TABLE NO.           TITLE                                             PAGE

  I                 SUMMARY OF EMISSIONS AND BURNING CONDITIONS         4-5

 II                 COMPARISON OF O>2 RESULTS                           9

III                 SUMMARY OF GASEOUS EMISSION CONSTITUENTS           10

 IV                 FUEL CHARACTERISTICS                               12

  V                 REPRESENTATIVE FIREPLACE MEAN DIMENSIONS AND       22
                    95% CONFIDENCE INTERVAL

 VI                 AUXILIARY FIREPLACE EMISSION DATA                  52
                            LIST OF FIGURES


  1                 AVERAGE FIREPLACE PORT LOCATIONS                   3

  2                 VALENTINE, FISHER & TOMLINSON STACK GAS SAMPLING   6
                    TRAIN WITH BACK-UP FILTER

  3                 ATMOSPHERIC EMISSION VARIATION WITH BURNING        7
                    CONDITIONS

  4                 ADSORBENT SAMPLING SYSTEM                         15

  5                 IMPACTOR PARTICLE SIZING TRAIN                    17

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         VALENTINE,  FISHER    &   TOMLINSQN
                                CONSULTING ENGINEERS
                                  A.ซ.H.It.A.B..A.A.A.ซ.. C.A.M.B.. I.B.*.

                         S20 LLOYD BUILDING   •   (20ซ)  623-0717
                              SEATTLE, WASHINGTON  98101
WM. M. VA^NT.NE. M.E.                                                        ASSOCIATES:
ARTHUR K. r,SHER. M.E.
CEORGE D. TOML.NSON, E.E.                                                     Dซป""8 *'
                                                                        HENRY U. ROYCE. IL.UUM.
SH. ASSOCIATE,                                                              WHJJAM T. MCOONAUO
WAYNE A. HANSON, M.E.                                                        OEAN A. HANNIO
DOUOUASW.*A*eOE.E.E.                                                       *OซEI* C. HUNTUEY
F. "CHIC" CICCHETTI                                                           WESIJTY O. SNOWDEN, *.E
                                  I.   INTRODUCTION                      INORU J. I-RIMUANI. M.E.


      This Atmospheric Emission  Evaluation was conducted on an "Average Fireplace"
      located in the Seattle  area for use in the development of an Emission Factor
      for residential fireplaces, EPA Contract No. 68-02-1992.  This Project  was
      funded by the United  States Environmental Protection Agency's National  Air
      Data Branch, Technical  Development Section, with Messrs. James A. Southerland
      and Tom Lahre serving as advisors  during the entire evaluation.  Messrs.
      David A. Alguard, Gregory  A. Swans on and William E. Stolberg, of Valentine,
      Fisher & Tomlinson, served as  project leader and colleagues respectively.
      The field sampling was  performed during the period of July 29 through August 20,
      1975.

      Area wide emissions can be projected from the enclosed point source  emissions
      factors by establishing the number and use frequency for residential fireplaces.


                                    II.  SUMMARY


      The average pollutant mass rate was found to be 76.1 grams/hour and  the grams
      of particulate per kilogram of wood burned was found to be 10.4 grams /kilo gram.
      The average particle  size  was  3.0  microns.  66. 3Z of the particulate was
      condensables caught in  the back half or impinger section of the Method  5
      sampling trains.  A back-up filter was used in anticipation of this  high back
      half catch.  All atmospheric emissions reported are calculated using front
      half plus back half particulate including the back-up filter.  Poor  combustion
      conditions of considerable excess  air was indicated by C02 concentrations  of
      consistently less than  1.0%.

                                               VALENTINE, FISHER & TOMLINSON
      WDS/lae                                  Wesley D. Snowden
                                               Manager, Environmental Services

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                 III.  DISCUSSION OF EMISSION FACTORS
The representative fireplace in the Seattle  area was  prepared for sampling
as shown on Figure 1.  The selection of  the  representative fireplace is
discussed in Appendix A.  A total of 24  samples consisting of 18 EPA Method 5
samples, 3 polycyclic organic material  (POM)  samples  and 3 particle sizing
runs were collected from the selected fireplace.   Sampling was performed
using alder, pine, douglas fir, locust and coal as fuels.   Coal was not
included in computing final average emission parameters  because of its current
low frequency of use.

A summary of emissions and burning conditions is presented in Table I.
Sampling was conducted under three burning conditions of start-up, stable,
and smolder.  Start-up conditions were present just after building the fire.
The flue gas temperatures were rising during this  condition.   Stable conditions
were present when the fire had reached a constant  combustion rate.  The flue
gas temperatures were at a constant level during this burning condition.
Smolder conditions were present when the fire was  no  longer stoked.  Since no
fuel was being added during smoldering,  burning rate  was decreasing.  Flue
gas temperatures dropped throughout the  smolder condition.

Emissions reported in Table I are calculated using the EPA Method 5 front
half section plus the back half section  which includes a back-up filter.  In
addition to the standard EPA-designed particulate  sampling train (referred
to generally as Method 5) a back-up filter was added  between the dry bubbler
and the bubbler containing silica gel.   The  sampling  train with the back-up
filter is shown in Figure 2.  The average back-up  filter catch for the
18 particulate runs was found to be 61%  as heavy as the front half filter
catch  (see Tabulation of the Ratio of Back Half to Front Half Catch,
Appendix B).  In four cases the back-up  filter catch  was more than the front
half filter catch.

Concentrations of C02 reported in Table  I were measured by an Orsat analyzer.
Subsequent particulate concentrations corrected to 12% C02 are susceptible
to errors due to the magnitude of correction and  the  accuracy of the C02
analysis.  More accurate determinations  of C0ฃ were made by infrared analysis
as shown in Table II.

The data given in Table I shows how three factors  affecting atmospheric
emissions were developed during this project. The factors are 7.4 kilograms
per hour wood burning rate  (BR),  76.1 grams  per hour  pollutant mass rate  (PMR)
and 11.7 grams emissions per kilogram of wood burned  (PMR/BR) .  The BR and the
PMR were calculated  from the average of  fifteen modified EPA Method 5 sampling
runs.   From these fifteen runs a  95 percent  confidence interval was found for
the BR, PMR, and PMR/BR to be + 1.15, + 11.6 and + 2.3 respectively.

All samples utilized  for emission parameters reported in Table I were
collected within 100 + 10% of isokinetic conditions.   Stack sampling utilized
3-foot heated glass  probes within S type pitobes.   A  1/2-inch diameter nozzle
was used to collect  all particulate and  POM  samples.   Section IV, Procedures,
describes in more detail the sampling procedure used  for this evaluation.

An important emission parameter which allows comparison of the emissions of
various  types of wood being burned, is  gm particulate/kg wood burned.  A plot
of this parameter versus burning  condition,  Figure 3, reveals that emissions

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                                                              SXTSUS10U
                                             UQ-SCALS
           :^B3ฃPUCฃ. . SAMPLING  PORT AOCAT/OA/S
FIGURE 1
                                            ฃ• M L
                                 CHECKED:
                                  q 4.5.
Pnpsrtd by:
VALSUTiue. FISHER
   Consul ring
   57Q LLOYD BlJlLDlUG
   SStTTLS,

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                  TABLE I
Summary of Emissions and. Burning Conditions

Fuel 'Type Run
Alder 1
Alder 2
Alder 3
Alder 4
Alder 5b
Alder 6c
Alder Average
Alder Average
Alder Average

Douglas Fir 7
Douglas Fir 8
Douglas Fir 9
Douglas Fir 10
Douglas Fir lie
Douglas Fir
Average
Douglas Fir
Average
Douglas Fir
Average
Locust 14
Locust 15
Locust 16
Locust 17b
Locust 18
Locust Average
Locust Average
Locust Average


*Burning
Conditions
Start Up
Stable
Smolder
Start Up
Stable
Stable
Start Up
Stable e
All
Conditions e
Stable
Stable
Start Up
Stable
Stable

Start Up

Stable
All
Conditions
Start Up
Stable
Start Up
Stable
Stable
Start Up
Stable
All
Conditions

Burning
Rate
Kg/hr (BR)
4.8
• 7.8
1.9
10.8
9.1
6.2
7.8
7.8e

6.3e
5.7
4.1
8.3
6.7
4.3

8.3

5.5e

6.2e
9.0
6.2
5.2
4.5
5.5
7.1
5.8d

6.5d

Stack
Temp
83
108
67
114
92
9*
m
108e

93e
79
88
83
110
88

83

92e

90e
86
92
82
91
91
84
92d

88d
Stack Gas
Fjlow Rat^e
Std.ซ
11,534
IQ.Sli
8.262
9.242
-*-.-b
12.771
10.39
10,513e

9.889e
12.139
11.715
8.787
11.814
11.737

8. 787

11.889e

11.114*
10.046
11.414
9.918
- — -b
12.709
9,982
12.062d

11.022d

pollutant
' Mass Rate
gnu/hr (PMR)
'"" 76.6
46.0
42.2
135 ,4
-• .--b
-*,-- c
106
46. Oe

75. Oe
65.7
58.9
72.7
90.2
-. — -c

72.7

71. 6e

71. 9e
85.2
78.7
60.4
— b
84.2
72.8
81. 4d

77. Id

**Concent-
ration
gm/std.m3
.111
.073
.085
.244
	 4>
	 c
.178
.073e

0.128e
.090
.084
.138
.127
-^-c

.138

.104e

.llOe
.141
.115
.102
,-- b
.110
.112
.112d

,117d

C02
0.1
0.6
0.1
0.6
___
0.5
0.4
0.6e

0.4e
0.2
0.4
0.6
0.4
0.5

0.6

0.3e

0.4e
0.4
0.4
0.6
— __
0.4
0.5
0.4d

0.4d
**Concent-
ration
gm/std.m3
@12%C02
13.279
1.389
10.211
4.690
	 b
	 c
8.984
1.389e

7.392e
5.414
2.322
2.759
3.817
	 c

2.759

3.851e

3.578e
.430
.397
2.150
	 b
3.312
1.290
1.854d

1.572d
Pollutant
Mass Rate .
Burning
Rate (PMR/BR)
gm/Kg
16.0
5.9
22.2
12.5
	 b
	 c
14.2
5.9e

14.15e
11.5
14.4
8.8
13.5
	 -c

8.8

13. le

12.05e
9.5
12.7
11.6
	 b
15.3
10.6
14. Od

12.3d

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Table I, Continued
Summary of Emissions and Burning Conditions

Fuel Type
Pine
Pine
Pine
Pine
Pine
Pine
Pine Average
Pine Average
Pine Average
Coal
Coal
Coal Average

All Types h

a) Standard
b) Particle

Run
19
20
21 c
22f
23
24b



12
13


Aver.

- 76 cm
sizing -
Burning
Conditions
Start Up
Stable
Stable
Start Up
Stable
Stable
Start Up
Stable
All
Conditions
Start Up
Stable
All
Conditions
All
Conditions
Mercury 21.1ฐ
see particle
Burning Stack
Rate (BR) Temp
Kg/hr
11.2
14.0
10.0
11.1
9.1
13.6
11. 2e
11. 6e
11. 4e
2.3
2.7

2.5

7.4
C and dry
ฐC
125
109
104
136
105
97
125e
107e
113e
80
74

77

95

Stack Gas
Flow Rate
Std. a
m3/min
11.857
10.986
10.539
8.484
10.727
	
11.857e
10.856e
11.190e
11.290
11.597

11.444

10.778

Pollutant
Mass Rate
gm/hr (PMR)
80.5
91.4
	 c
151.5
73.9
	
80. 5e
82. 6e
81. 9e
69.8
38.8

54.3

76.1

Concent-
ration
gm/std.m3
.113
.139
	 c
0.298
.115
	
.113e
.127e
.122e
.103
.056

.080

.119


Concent-
Pollutant
Mass Rate
ration Burning
% gm/std.m3 Rate(PMR/BR)
C02
0.2
0.2
	 c
l.Of
0.5
	
0.2e
0.4e
.3e
0.2
0.3

0.2

0.4

<ง12%C02
6.792
8.323
	 C
3.572
2.755
	
6.792e
5.539e
5.957e
6.186
2.231

4.208

4.536

gin/Kg
7.2
6.5
	
13.6
8.1
	
7.2e
7.3e
7.3e
30.3
14.4

22.4

***!!. 7

sizing results
c) Sampling for polycyclic organic materials (POM) - See Table II
d) Particle sizing runs not included in average
e) POM; particle sizing, smolder and glass front, (if run) are not included in average
f) Glass fireplace screen was used for this run - note higher % C02
g) POM runs are not included in average
h) Coal, POM, particle sizing and glass front runs are not included in average
 * Start Up - Initial ignition of fire or fuel addition, increasing combustion rate.
   Stable - Constant combustion rate.
   Smolder - Tail end of combustion, decreasing combustion rate.
** All values reported from results of modified EPA Method 5; front half, back half
   impinger catch, and back-up filter.
***Statistically determined mean from
   individual values or PMR/BR. Division
   of mean PMR by mean BR is not equal
   to the mean of the individual EMR/BR
   values due to statistical procedure
   for obtaining mean values

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                                             HEATED BOX
  "S" Type pitot
  integral with
                                                                                            TEMPERATURE
                                                                                                 UMBILICAL
                                                                                                 CORD
FIGURE 2
L
                    VALENTINE, FISHER & TOMLINSON STACK GAS SAMPLING TRAIN WITH BACK-UP FILTER

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     30 --
•K
     25 --
o
UJ

UJ
1

     20 --
     10 --
o
ex.
      5: •-
	1—
 START-UP
A - ALDER

C - COAL
D - DOUGLAS FIR

L - LOCUST
P - PINE

  subscripts identify emission
  points from same fire or burn
                                                              +
                                         STABLE
   SMOLDER
                                  BURNING CONDITION
     FIGURE 3
                                ATMOSPHERIC  EMISSION VARIATION
                                    WITH  BURNING  CONDITIONS
         **Emissions were calculated using front half and back  half  particulate
           collected in the EPA Method 5 type sampling train.

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are mainly grouped within  a  range  of  from 5.9  to 16 grams of particulate
per kg \K>od burned.  No  general  trend of  emissions at the various burning
conditions for all species can be  observed from this plot.  Emissions from
pine wood and alder burning  decrease  from start up to stable burning while
douglas fir and locust increase.   Only one sample was obtained during
smoldering as it was observed during  testing that the stack gas opacity was
so low and little fuel was being consumed.  In retrospect, more samples
should have been taken during this burning mode.  These erratic results
would indicate that emission trends cannot be projected simply from factors
such as wood species and burning conditions.  Other factors which might be
included in the final emission factor development might be moisture content
and density of the fuel  and  temperature of combustion.  Also, nebulous factors
such as fire stoking technique and fuel configuration (e.g., split or unsplit)
could cause some variability.

The back half of the EPA Method  5  sampling train (impingers and back-up filter)
caught more particulate  than the front half (filter and probe).  The back half
particulate catch was an average of twice the front half catch, indicating
that fireplace burning is  a  partial combustion process releasing a significant
portion of vaporized hydrocarbons  (See Appendix B).  The back half particulate
catch appeared as a golden coloration of the condenser water and as a similar
color on the back-up filter.

During the field sampling  phase  of this project, we expected to use
particulate collected in the front half (i.e.  probe and filter) of POM
sampling to project a total  particulate catch.  When analysis was completed, it
became obvious that no general relation between front half and back half
particulate developed as projected (see Appendix B).  Consequently, POM
samples are not used  in  the  determination of average particulate parameters.

The  flue gas was. analyzed  to quantitatively determine various components.
These  components are nitrogen  (^), oxygen  (02), carbon dioxide (C02), carbon
monoxide  (CO).  Gas analysis and determinations of ^, 02, CO, C02 and dry
molecular weight of the  stack  gas were performed according to EPA Method 3,
Federal Register.  December 23,  1971,  Sections 3.2, 3.3 and 4.3 (see Section IV
for  procedures).

 In addition  to  in-the-field Orsat determinations of N2, 02, CO and C02,
more accurate  determinations were made in the laboratory using gas chroma-
 tography  (GC)  and  infrared spectrophotometry  (IR).  Three runs, 6, 8 and 15,
were selected  for  the  analysis  of these parameters.  GC methods were used
 to quantitatively  determine the  N2 and 02 values for these runs.  CO and
 C02  quantities were determined  using IR.  The values of these emission
 constituents  can  be found  in Table III.  Non-methane volatile hydrocarbons,
 (NMVH), were  also  quantified (see Table III), using infrared spectophotometry.
 Hexane was  used  as a  standard  and all results are read as Hexane.  The average
 NMVH was  found  to  be  4.8 ppm.   (See Appendix C  for GC graph and Appendix D
 for IR graph.)

 A good indicator  of the  accuracy of Orsat analysis is to compare the quantites
 of C02 obtained  by Infrared (IR) analysis, with those obtained by Orsat
 analysis.   It  can be  seen in Table II that  the  difference in % C02 is significant,

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                               TABLE II

                       COMPARISON OF C02 RESULTS
Run No.
6
8
15
% C02
Infrared
(IR)
0.63
0.79
0.65
% co2
Orsat
0.5
0.4
0.4
Difference
0.13
0.39
0.25
The lower Orsat measured carbon dioxide concentrations at 0.4%  indicates
that combustion of wood in a fireplace is taking place with 4900%  excess  air
(See Appendix F for % excess air calculation)0  Carbon dioxide  was calculated
at 1% theoretically which yields 1900% excess air.  In either calculation,
the high excess air quantities indicate that fireplace burning  of  wood  is at
best a partial combustion process.

One sample was taken with a glass front fitted on the fireplace to determine
the effect of reduced air supply to the fireplace.  Carbon dioxide was  increased
indicating more efficient combustion but atmospheric emissions  were not
significantly reduced.

Three POM samples were collected, one each, on alder, douglas fir  and pine
fires.  POM concentrations in the stack gas averaged 6,946 ng per  cubic meter
(76 cmHg and 21.1ฐC dry).  The complete results showing each constituent
analyzed is shown in Appendix E.  The procedure of POM sampling and analysis
is discussed in Section IV.  The total concentration of POM in  runs 6,  11
and 21 are shown in Table III.

Three cascade impactor particle sizings were made, (one each),  on  alder,
locust, and pine wood using a Brinks particle sizer built into  the Method 5
type sampling train (see Figure 5 in Section IV).  The mean particle sizes are
3.5 microns, 2.2 microns, and 3.4 microns respectively.  The average particle
size for the three runs (Nos. 5, 17 and 24) is 3.0 microns.  The particle size
samples were collected at 358, 385 and 269% of isokinetic conditions for  runs 5,
17 and 24 respectively.  These high % of isokinetic values are  due to under
sizing of the sampling nozzle.  The stack gas velocity was 7.8  feet/sec,  at  the
point of sampling.  The nozzle was sized by previous sampling experience  where
approximately 25 feet/sec, is normally encountered.  (Procedures of particle
sizing runs are found in Section IV.  Calculations and distribution graphs are
found in Appendix G.)

Precautions were taken to maintain uniform burning conditions during sampling.
Stack gas temperatures were revealed during sampling to provide a  good  indi-
cation of the state of combustion conditions.  As stack gas temperatures  dropped,
more fuel was added which maintained the stack gas temperature  within a
relatively constant range.  A "P" type pitot at a single reference point  was
utilized to attempt to monitor flue gas flow changes during sampling.   The
reference pitot also would have allowed corrections to be made  in  the flue gas

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                                                    TABLE III
Summary of Emission Constituents
Concentration
Polycyclic Polycyclic
Organic Organic

Fuel Type
Alder
Douglas Fir
Douglas Fir
Locust
Pine
All Average

R-in
6
8
11
15
21

Burning
Condition
Stable
Stable
Stable
Stable


Materials a
(ng)
166,000
	
220,000
	
162,000
183,000
Materials
ng/sitd. m3 b
5,746
	
7,444
	
7., 647
6,946
Parameters Obtained by Gas
Chormatography and Mass
Spectopho tome try
%
02
20.2
20.0
	
20.2
	
20.1
%
N2
79
79
—
79
—
79
PPM
CO
280
405
	
440
	
375
PPM
C02
6,300
7,900
	
6,500
	
6,900
PPM
NMVHc
4.5
4.7
	
5.3
	
4.8
a) See table V for quantification of specific materials
b) Standard - 76 cm. Mercury 21.1ฐC and dry
c) WMVH - Non Methane Volatile Hydrocarbons

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flow recorded during traverse sampling if  the  flow fluctuations would have
been significant.  The procedures used in  sampling and  calculations involving
the reference pitot are found in Section IV.   Example calculations of a
velocity correction coefficient  (See Appendix  H)  indicate that three of
the most variable samples required an average  air flow  adjusted increase of
2.2%.  Therefore, the resulting correction  in  total air flow from the flue
gases for all runs would be less than 2.2%.  With this  correction so slight,
a correction was not made in reported flows.

A special expanded inclined manometer (24  inches  long)  was  utilized to obtain
precise stack pitot readings.  The velocities  of  the stack  gas averaged 2.15
meters per/sec, on 20 runs, with such low velocities the expanded manometer
was most useful.

Wood burning rates, (tabulated in Appendix  I), were determined from data collected
during sampling runs.  The wood burning rate for  all types  of  wood in the
particulate samples excluding one smolder run  and the glass  fireplace screen
run was 7.4 kg per hour.  Procedures for determining fuel consumption rates are
found in Section IV.

The ultimate heating efficiency of the reference  fireplace was determined in
an energy balance found in Appendix F.  The efficiency  at 70ฐF outside tempera-
tures was determined to be 30%.  With lower outside temperatures,  this efficiency
will decrease.

The moisture content and density of the fuel consumed during this  pro/ject are
found in Table IV.  The average moisture content  of  the  wood fuel  was 12.5%.
The wood fuel density averaged 0.52 grams per  cubic  centimeter.   The fuel
analysis procedures are found in Section IV.

Two projects separate from this report were previously  performed  by Valentine,
Fisher & Tomlinson.  The atmospheric emission  parameters of  these  projects  are
found in Appendix J.

-------
                                   TABLE IV

                             FUEL CHARACTERISTICS
                                        Dry Density         Wet  Density
Fuel Type           Percent Moisture    grams/cc            grams/cc
Alder
Fir
Locust
Pine
Coal
12.2
10.6
11.7
15.4
	 	
0.43
0.39
0.64
0.36
1.18
0.49
0.44
0.73
0.43
_—__
                                              12

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                            IV.  PROCEDURES
PARTICULATE SAMPLING TRAIN

Stack gas sampling equipment designed by the United States Environmental
Protection Agency, (EPA), Office of Air Quality Planning and  Standards was used
on this evaluation.  A schematic of the sampling equipment is shown in Figure 2.

Sampling was performed according to the following:
The number of sampling points were determined by considering  the number of
duct diameters between obstructions in the duct upstream and  downstream of
the sampling ports.  The rectangular chimney 8.75 in. x 19.25 inป  had  an area of
1.17 ft2 and was equivalent in area to a round duct 1.22 ft.  in diameter or
by equation 1-1 of Method 1 Standards of Performance for New  Stationary
Sources, i.e. 2 (length) (width) or the chimney was equivalent to  a round duct
              (length + width)
1.0 ft. in diameter.  Thus the number of stack diameters downstream from the
damper was 15, and the number of diameters upstream from the  chimney top was
1.8.  The minimum number of points required would be 10.  The actual number of
points selected was 20 to improve air flow measurement and sampling accuracy.
A drawing of the fireplace port locations is shown on Figure  1.  The five
ports A, B, C, D and E are spaced 3.85 inches apart and ports A and E  are
1.92 inches from the inside wall of the chimney.

Five ports with 4 sampling points each giving 20 points total were required in
order to meet criteria from the Federal Register Method 1 Section  2.2.2.  The
ratio of the length to width of each elemental area was 1.76  meeting the 1 to 2
ratio requirements.

Stack pressure, temperature moisture content and maximum velocity  head readings
were measured.  An EPA designed nomograph was set up using this data and the
correct nozzle diameter was selected using the nomograph.

The sampling train was prepared as follows:
A filter (MSA 1106-BH) was labeled and desiccated for at least 24  hours to a
constant weight and weighed to the nearest 0.5 mg.  The filter was placed in a
glass holder and was supported by a glass frit.  The outlet side of the filter
holder was connected to the condenser section.  100 miligrams of water was
placed in the first bubbler and second impinger.  The third bubbler was left
dry.  The fourth bubbler was filled with approximately 500 gram of silica gel.
All four sections of the condenser were then weighed individually  to the nearest
0.1 gram and recorded.  A back-up filter (MSA 1106-BH) was desiccated  for more
than 24 hours to a constant weight and weighed to the nearest 0.5  mg.   The back-up
filter was placed between the third and fourth bubblers.

Just prior to sampling, a leak test was performed on the assembled sampling train.
The leak rate did not exceed 0.02 cfm at a vaccum of approximately 24  inches Hg.
The probe was,heated so that the gas temperature at the probe outlet was approx-
imately 2508F.  The filter was heated to approximately 250ฐF  to avoid  condensa-
tion of moisture on the filter.  Crushed ice was placed in the condenser section
at the beginning of the test with new ice being added as required  to keep the
gases leaving the sampling train below 70ฐF.

-------
The train was operated as follows:
The probe was inserted into  the  stack to  the first traverse point with the
nozzle tip pointing directly into  the gas stream.   The pump was started and
immediately adjusted  to  sample at  isokinetic velocities.   Equal time was spent
at selected points of equal  elemental areas of the duct with the pertinent
data being recorded from each time interval.  The  EPA nomograph was used to
maintain isokinetic sampling throughout the sampling period.  At the conclusion
of the run the pump was  turned off,  the probe was  removed, and the final
readings were recorded.

Clean up of the  sample train and analysis of the samples were performed according
to the Clean-Up  and Analysis procedure found on page 18.


POLYCYCLIC ORGANIC MATERIALS

The Polycyclic Organic Materials (POM) determined  by the consulting laboratories
of Batelle Columbus Laboratories,  Columbus, Ohio,  were sampled as follows:

Sampling was conducted by Valentine, Fisher & Tomlinson's Environmental
Services Team.   Sample collection was made at isokinetic conditions at
all preselected  traverse points.  The sampling system was a modified EPA
Method 5 sampling  train  using a  special POM adsorbent column of Tenax
 (see Figure 4).  The  column  was  located directly after the heated filter.
Prior to passing through the adsorbent, the gas was cooled to 55ฐC in a
thermostatically controlled  circulating water bath.  From here the gas
entered the regular EPA  condenser section.

Aluminum foil was  wrapped around the Tenax column to prevent light exposure.
After sampling,  the Tenax column and cooling jacket were removed from the POM
 train and  sealed with a  Solv-Seal cap and a ball-joint stopper.  This section
was stored out of  light  prior to shipment to Batelle Laboratories for analysis.
The tared  acid treated glass filter was removed and desiccated until a constant
weight was obtained.  The filter was weighed to the nearest 0.1 mg.  The
 impinger section was  weighed and the amount of water collected was determined.
The probe  and prefilter  connections were cleaned up with brushes and reagent
 grade acetone.   The washings were transferred to a tared beaker and after
 evaporation and  desiccation  the  net weight gain was determined.  The filter
 and Tenax  column section were shipped in padded containers to Batelle for analysis,
 Gas chromatographic  separation was utilized to quantify the POM constituents.

More  detailed  sampling and  analysis procedures can be found iii "Efficient
 Collection of Polycyclic Organic Compounds From Combustion Effluents," by
 Peter W. Jones et. al, Paper No. 75-33.3, Batelle Columbus Laboratories,
 505 King Avenue, Columbus,  Ohio   43201, presented at Annual Meeting of Air
 Pollution  Control  Association in Boston, Mass., June 1975.
 llT.ll
  P" TYPE REFERENCE PITOT

 The "P" type reference pitot was positioned 9" below point C-3 during
 each particulate 'and POM sampling runs to correct for total air flow but
 sampling revealed the correction to be unnecessary.  Reference pitot readings
                                            14

-------
               FLOW DIRECTION
                                                      RETAINING SPRING
                    8-MM GLASS
                    COOLING COIL
                       GLASS FRITTED
                       DISC
GLASS WATER
JACKET
FRITTED STAINLESS STEEL DISC-

    15-MM SOLV-SEAL JOINT
                  ADSORBENT SAMPLING SYSTEM

        From  the Paper:  Efficient Collection of Polycyclic
        Organic Compounds from Combustion Effluents, by
        Peter W. Jones et.al.
                           FIGURE  4

-------
were made during each  sampling  point time interval.  The method by which the
velocity could have been  corrected for a particular run is as follows:

The average square root of  all  reference pitot readings ratioed over the
square root of each particular  reference reading yielded the pitot correction
coefficient for each point  on the stack traverse.  Each traverse pitot reading
was corrected by calculating the product of the pitot correction coefficient
times the traverse pitot  reading.  The ratio of the average of all corrected
traverse pitot readings over the average of all traverse pitot readings
yielded the stack velocity  correction coefficient.  The velocity calculated
from  the actual data can  then be corrected by this coefficient.  (See three
examples in the Appendix).


INTEGRATED GRAB BAG GAS  SAMPLING

An integrated  sample of  stack gas was taken for each run during the evaluation
according to the following  method.  A probe was inserted into the stack.  In
line  with the  probe was  a drying tube which contained glass wool and silica
gel to remove  particulate and moisture.  This assembly was connected to a
sampling pump  inlet.   All connections were checked for leaks and the sampling
line  was purged.  An evacuated flexible aluminized scotchpak (polyvinyl
chloride) bag  was  then connected to the pump outlet and an integrated sample
was taken at a rate proportional to the stack flow rate.
 PARTICLE SIZING

 Particle sizing was accomplished using a cascade impactor as set up in the
 sampling train'shown in Figure 5.

 The Brinks Cascade Impactor consisted of five stages,-each of which
 contained a collection cup and a nozzle jet.  Particles suspended in the
 sample gas passed through the jet and were impacted on the disk.  The
 amount of particles collected on each disk was a function of the gas
 velocity through the jet, the particle characteristics, and the amount
 of sample drawn.

 The sampling train is set up as in the drawing.  The nozzle tip diameter
 was essentially the only means of providing for isokinetic sampling.
 A 0.125 in diameter nozzle was utilized in sampling.  The sample flow rate
 was fixed by the pressure drop across the impactor  (pressure drop is
 determined by the 3rd impactor stage, and its requirements for maximum
 collection).  With the normally small flow rates, a 0.125 inch nozzle tip
 was necessary to prevent under isokinetic sampling  (unrepresentative large
 particle capture).

 The sample train was leak tested under 24 inch mercury vacuum.  A leak test
 of 0.02 cubic feet per minute was obtained.  The probe and the sample box
 were heated to 250ฐF.  The sample probe was inserted in the process stream
 and gas flow through the impactor was started and held near constant until
 the end of the test.  The vacuum was held constant at 5.0 inches of mercury,
 Sampling time was 20, 30 and 30 minutes on runs 5, 17 and 24 respectively.
                                          16

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FIGURE 5
OATI
VALENTINE, FISHER & TOMUNSON
    CCM'i'Ji.IIMG ENGINCtRS
   520 IIOYO BlUG., SEATTLE
                                                                                                      6wo.ua

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After each test, the  sample  cups  were removed from the impactor with tweezers.
The quantity collected on  each  cup  was determined by weighing to the nearest
0.1 mg after desiccation.  Similarly, the quantity of material collected on
the filter was determined.   The nozzle,  probe and pre-filter connections were
rinsed with reagent  grade  acetone.   The nozzle and probe washers were evaporated
to dryness in a  150 ml tared beaker.  The prefilter connections wash was also
evaporated to dryness in a tared  beaker.  The weight of residue in both beakers
were determined.  A blank  value for the acetone used was also determined.
CLEAN-UP AND ANALYSIS

Clean-up of the  EPA train was performed by carefully removing the filter
and placing it in a container marked Sample #	 A.  Reagent grade
acetone and brushes were used to clean the nozzle,  glass probe and
pre-filter connections.   The acetone wash was placed in a container marked
Sample #	 B.   The impinger and bubblers were weighed in their respective
containers to  the nearest 0.1 gram.   The original weights which included
approximately  100 ml water in one bubbler and 100 ml water in the impinger
were  then subtracted and the differences added with the water weight gain of
the silica gel.   This  constituted the amount of water collected during the
run.  The silica gel was weighed in  a bubbler before and after the run.  The
water from the glassware and a water rinse of the glassware were placed in a
container marked Sample  #	 C.  An  acetone rinse of the glassware and all
post-filter glassware  (not including the silica gel container) was performed
and placed in  a  container marked Sample #	 D.  The back-up filter was
carefully removed and  placed in a container marked Sample #	 E.

Analysis of the  samples  in each container was performed according to the
following:

Sample #	 A  -  Transfer the filter  and any loose particulate from
the sample  container to  a tared glass weighing dish and desiccate
for 24 hours in  a desiccator containing "drierite."  Weigh and redesiccate
repeating until  a constant weight is obtained and report the results to
the nearest 0.1  milligram.

Sample #	 B  -  Measure  the volume to the nearest 0.1 milliliter.
Transfer acetone washings from container into a tared beaker and
evaporate  to dryness at  ambient temperature and pressure.  Desiccate
for  24 hours and weigh,   redesiccate and weigh repeating until a constant
weight is obtained. Report the result to the nearest 0.1 milligram.

Sample it	 C  -  Measure  the volume to the nearest 0.1 milliliter.  Extract
organic particulate from the water solution with three 25 milliliter portions
of chloroform  and three  25 milliliter portions of ethyl ether.  Combine the
ether and  chloroform extracts and transfer to a tared beaker.  Evaporate
until no  solvent remains at about 70ฐF.  This can be accomplished by blowing
air  that  has been filtered through activated charcoal over the sample.  Desiccate
for  24 hours and weigh and redesiccate to a constant weight.  Report the results
 to the nearest 0.1 milligram.  After the extraction, evaporate the remaining
water to  dryness and report the results to the nearest 0.1 milligram.

-------
Sample #	D - Measure the volume to the nearest  0.1 milliliter.   Transfer
the acetone washings to a tared beaker and evaporate to  dryness at ambient
temperatore and pressure.  Desiccate for 24 hours  and weigh to a constant
weight.  Report the results to the nearest 0.1 milligram.

Sample #	 E - Transfer the filter and any loose  particulate  from
the sample container to a tared glass weighing dish and  desiccate
for 24 hours in a desiccator.  Weigh to a constant weight  and  report the
results to the nearest 0.1 milligram.

Blanks were taken on the acetone, ether, chloroform, and deionlzed water
and subtracted from the respective sample volumes.  The  filter paper used
with the EPA train was a Mine Safety Appliance 1106 BH,  heat treated glass
fiber filter mat.
FUEL DENSITY AND MOISTURE CONTENT

Samples of each type of wood fuel were determined for moisture by weighing
samples of each and drying these at 105ฐC. for several days.  After  cooling
in a desiccator the samples were weighed.  This process continued until
constant weights were found.  The % moisture was calculated by dividing the
weight lost by the original weight times 100.

The densities of all fuels including coal were determined by weighing  samples
of each and then measuring the liquid displacement of each sample.   Density
was calculated by dividing the weight by the displaced volume.


WOOD WEIGHT AND FIRE STOKING

Prior to sampling, the fire was built with a weighed quantity of fuel.   The
wood was weighed with a spring balance.  With this data the fire stoker
would estimate the quantity of wood in the fire at the start of sampling
and record the estimate on the data sheet.  As wood was required for the fire,
it was weighed and placed on the fire.  The time and weights of the  wood
added were recorded on the data sheet.  At the end of sampling the stoker
would estimate the quantity of wood left in the fire and would record  this
data.  Each day of sampling was begun with the fireplace swept out.  A hearth
of ribbed cast iron was used throughout the evaluation.


GAS ANALYSIS

On runs 6, 8 and 15, nitrogen and oxygen were analyzed utilizing thermal
conductivity gas chromatography techniques.  A 20-foot long 1/4-inch
diameter 45/60 molecular sieve column at 100ฐC and an attenuation of 16 X
was used for this determination.  The carrier gas was Helium at 50cc/minute.
A 0.25 milliliter sample was injected into the G.C.  Three representative
G.C. peaks per parameter for each run analyzed substantiated the reported
values as measured against standard N  and 02 peaks.
                                          19

-------
Carbon monoxide, carbon dioxide, and non-methane volatile  hydrocarbon were
analyzed by means of an infrared spectrophotometer with  a  10 meter  cell.
Standard curves for CO, CO2, hexane and methane were  run.   The  value  for
methane was determined for each run analyzed,  then subtracted from  the
total volatile hydrocarbon value measured  as hexane,  resulting  in the reported
quantity of total volatile non-methane hydrocarbons.

All runs except particle size runs and POM run #21, utilized the hand-operated
Orsat for quantifying oxygen, carbon dioxide,  carbon  monoxide and nitrogen
concentrations in the stack  gas.  The samples  were collected as described
in the preceding procedure in integrated grab  bag.  In analysis CO 2 was
absorbed in the first column of the analyzer.  The gas sample was passed
through the column  several times to insure complete collection. The  volume
of displaced gas was recorded.  Oxygen and then carbon monoxide were
measured similarily.  In all cases of quantifying the gas  constituents of
the grab bag sample at least three separate samples were pumped into  the
Orsat for separate  analysis. Nitrogen was quantified by subtracting  the
total percent of the measured gases from 100.
                                                 20

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SECTION IV




 APPENDIX
                21

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                               APPENDIX A
               SELECTION OF THE REPRESENTATIVE FIREPLACE
                    WITH STATISTICAL CALCULATIONS


The representative fireplace was selected from a  sample distribution  of  34
fireplaces.  The 34 fireplaces were  selected  from employees,  friends  and
relatives of Valentine,  Fisher & Tomlinson, Inc.  Wider and more  statistically
random selection of the  fireplaces was  limited due  to U.S. Government, Office
of Management and Budget  solicitation form approval procedures  and  contract
funding limitations.  Valentine, Fisher & Tomlinson is confident  that the
fireplace selected is of  a representative nature.


The fireplace dimension  parameters included in the  sample were  those  considered
to have an effect on the quality of  burning in a  fireplace.   The  parameters
included were:   (a) area of the fire box opening,  (b) cross sectional area of
the chimney opening and  (c) chimney  height.   These  dimensional  parameters are
illustrated in Figure 6.

From the compilation of  the 34  sets  of  parameters,  a population mean  was compute
for each parameter.  A  standard deviation was then  computed which was used to
determine a 95 percent  confidence interval for each mean dimension.   No  fireplaci
fit within a 99 percent  confidence interval.

Fireplaces were picked which had dimensions which were within the 95  percent
confidence intervals.   Three fireplaces were  examined more closely  and a final
selection was made based on accuracy of dimension,  accessibility  for  sampling
and consent of the owner.  The fireplace selected has an opening  of 6187 sq. cm,
a chimney cross sectional area of 1087  sq. car- and  a chimney  height of 4.66  m.
Note that the  chimney height was selected so  that a 0.46 m extension  could be
added and still remain within  the 95 percent  confidence interval  of chimney
height.
                                Table V

           Representative  Fireplace  Mean Dimensions  and 95%
                           Confidence Interval

Parameter                Mean  Dimension            Confidence Interval

Fireplace  Opening       6336  cm2                  5865 to 6807  cm
Chimney  Opening          961 cm2                   832  to 1,090  cm
Chimney  Height           4.4 meters                3.87 to 4.97  meters
                                          22

-------
                    MO SCAL5
FIGURE 6
                                  W.&.
                                  G-i5.
                                OATtt
                                '
                                                  u
                                             Consulrin
                                                     FISHER
BUILDING

-------
                                   APPENDIX B


                   Tabulation  of  Front Half to Back Half Ratios


      This tabulation of the front  half to the back half ratios  in  18 runs show the
      significance of the back half participate.  Also,  the back-up filter shows to be
      important in this type of sampling.
                                                 r>~,.     &UF,
                                                 /Tar/a,:  —=—
                                                         &
.5!.


 7
                                                           /• 32
                                                          ^LL^JL.
/o
//

i : • i : : — j . ! ; : —
                                                           .0
/ 3
Ma
                                                           ->
,20_

i..02i.8.

 /, 0*7
 '22
 ,047
                                                        	
-------
APPENDIX C
                           	.  O

-------
  .9
                             Ul
*
                                                   10  METE
                                                   INFRARED
                                   CELL
                                  SPECTROP
                       BECKMAN  IR-4
                       SAMPLE
                                     lOTOMETEfi
                                                         APPENDIX D	

                                                 jhfrered Speccrephotemet*
                             
-------
Table V
                                APPENDIX E
Fireplace Atmospheric Emissions
POM Quantification

POM QUANTIFICATION (ng)
POM quantification is reported in nanograms. The samples were collected by th
methods described in the Procedure section, Page 13.

NAS
Component Notation
Anthracene/Phenanthrene
Methyl anthracenes
Fluoranthene
Pyrene
Methyl Pyrene/ Fluoranthene
Benzo(c)phenanthrene ***
Chrysene/Benz (a) anthracene *
Methyl chrysenes *
Benzo fluoranthenes **
Benz(a)pyrene — *** —
Benz(e)pyrene
Perylene
-Mehtylcholanthrenes ****
Indene(l,2,3-cd)pyrene *
Benzo (ghi) perylene
Dibenxo( a, h) anthracene ***
Diebenzo(c,g)carbazole ***
Dibenz(ai and ah)pyrenes ***
Coronene
SAMPLE
Alder D. Fir Pine
69-5 76-5 8605
52,450 59,600 52,100
21,300 32,900 	
16,100 27,200 21,400
18,900 24,700 21,750
17,800 13,400 450
4,300 3,800 2,450
11,900 17,800 7,950
5,300 9,200 28,300
5,400 7,300 3,000
"1,200 8,900 12,400

	 	 	
3,300 9,600 5,650
1,300 2,600 3,050
2,800 3,200 3,000
	 	 	
	 	 	
	 	 	
	 	 	
TOTAL 166,000 220,000 162,000
                                           27

-------
                              APPENDIX F

                     ENERGY BALANCE, % EXCESS AIR


In order to evaluate the combustion characteristics  and  heating  efficiency of
the fireplace during testing, calculations were  done to  determine air  require-
ments for burning, % C02ป theoretical heat available,  and  heat losses  from the
fireplace.  These calculations are contained in  this section.

Combustion calculations were based mainly.on stoichiometric  equations  of combustic
and. the ultimate analysis of- wood.  The heat available for combustion  was also
calculated with data from ultimate analysis.

Heat losses from the fireplace were divided into four components.  These compo-
nents include:  heat lost in exhaust gases, heat lost due  to air infiltration,
heat lost from the fire box, and  heat lost from  the  chimney. Each of  these
components were then calculated using approximate  thermodynamic  and heat transfer
equations and techniques.
                                              28

-------
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                                                             uป &•

-------
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                                        3.
                  30

-------
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                        C ซ /c u /*ป-/•ซ. ^  C C -
31

-------
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                                                  32

-------
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                                  35

-------
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                                 36

-------
                              APPENDIX G

                            Particle Sizing

Particle sizing was performed by a Brinks Cascade Impactor.  The  samples  were
collected and determined by the methods found in the Procedure section, Page 15.
This appendix contains Particle Sizing Calculations, Secondary Data  and Size
Distribution Graphs.  Field Data and Moisture Determination is found  in Appendix  L.
                      CASCADE IMPACTOR CALCULATIONS



 VQ  -      (8465.41)0701^)   (Pm)  / (Tffl)  (TIME)  + (22.6417) (VOL,,) / (TIME)


 a   =       (234.0)  (/I2) /  (/>)   (P2)


 b   =       (2.05 x  108)  (yu.)   (P2)   /   (/p)   (V0)   (P0)

 Dpc=      J a + bDc3  -
 V0 =ป      Gas flow  at  inlet to  Impactor at 25ฐ C. and 14.7 psia,
          cc per  second.
          Dry gas meter volume at meter temperature and pressure, dry acf

 Pm ป      Dry gas meter pressure, "Hg

 Tm ป      Dry gas meter temperature,  ฐR

 TIME*     Sampling  time,  minutes

 VOI^ ซ     Volume of water collected, ml

 r "      Viscosity of gas  in impact or, gm / (cm) (sec)

 y ป      Density of gas  in impactor, gm per cc

 ?2 a      Average pressure  in impactor, atm.

 rn •      Density of aerosal particle,  gm per cc
  P                         /
 PO =      Pressure  at inlet to impactor,  atm.

 D =      Characteristic  diameter of  aerosol particle for impactor
          stage, microns

 Dc •      Diameter  of impactor jet, cm.
                                             37

-------
VALENTINE, FISHER &TOMUNSON
CONSULTING ENGINEERS
COMPUTER PR!NT-OUT OF ATMOSPHERIC EMISSION DAT)
JOB NAME
                                   APPROVED.
                     DATE-

                     PAGE,
SUBJECT.
                                                                  OF.
                       RUN NO.
       RUN NO.Z.
RUN
          VOL,
TIME
VOLW

2


2 -28
9-813
533
L. (j ,
2 •
25


757
•72
535
30
2-416
29-79
548
30
                             o • 6
                       54-659056
                26
          63-217313
           1 • 6
    33 - 26G256
ซ
P
i
a
b
DC
Dpc
DC
DC
Dpc
DC
Dpc
DC
Dpc
C • 6 0 o 7
0-9963
0-000275
0 • 0008527
0-9146
0-021645
1555-472020
0-245
4-755430
0- 1775
2-805816
0-1356
1-915043
0-0946
1-005413
0-0731
C • 6455 1C
0 • 6087
C • 9 9 3 3
C • 000275
0-000861
0-9131
0-021623
1346-744274
G-249
4-415042
C- 1775
2 -601155
C • 1 396
1 • 772527
0-0546
C • 5~3 0 4 3 5
0 • 0731
0-592448
C • 6037
0-5956
C • 00021
0-OGCS471
! 0-9142
0-012911
.1697-022253
0-249
5-006094
0-1775
2-965012
C • 1396
2-037841
0-0546
1-069548
C • 0731
C • 707805
                                               38

-------
Client
             . A .
                             CASCADE IMPACTOR DATA
Sampling Location   AVE"ffAC*L

Date  *Ju/\/  3O j >

Run Number  5
Comments
PARTICULATE
FINAL
(gm)

TARE
(gm)

NET PARTICULATE
(gm)
Cyclone

Stage #1

Stage #2

Stage #3

Stage #4

Stage #5

Filter (I/&-S"
ฃ*" AZ*,      -^iVM^^^
r ' f'r^ft^ j( . j
      '/o /
TOTALS

MOISTURE



Bubbler (#1)

Impinger (#2)

Bubbler (#3)'

Bubbler (#4)

TOTALS
                             3.
                                          -   3.2.^7?
                            3- ^ 
-------
                           CASCADE IMPACTOR RESULTS
Client:
Sampling Location:
Date:
                    /ซ97-T~
Run No:
Dp (=Dpc) , Particulate
ITEM microns collected, mg
Cyclone 2. . . ^^^ ^-^
/- 9
Filter
Weight % Cumulative %
collected less than Dp
+0.0
8.3 JT/ - 8
6.7 ^^ l
S'.O ^t-o. I
t -r ^^^ ^p
<*• 7 3J. 7
3/. 7
                                              40

-------
     99.99       99.9 99.8
                                                                                 1    0.5    0.2   0.1 0.05    0.01
             60   50    4O    30    20
'   0.01    0.05  0.1  0.2    0.5    1
10
20     30    40    50    60    70     80
                                                         90      95       98    99
                                                                                  99.8 99.9       99.99

-------
Client

Sampling Location

Date
                             CASCADE IMPACTOR DATA
Run Number
Comments
PARTICULATE
Cyclone

Stage #1

Stage #2

Stage #3

Stage #4

Stage #5

Filter  (

TOTALS

MOISTURE
 Bubbler

 Impinger  (#2)

 Bubbler  (#3)

 Bubbler  (#4)

 TOTALS
                              FINAL
                                (gm)
                   TARE
                   (gm)
3.
. 3
                              FINAL
                                (gm)
                   TARE
                   (gm)
             NET PARTICULATE
                   (gm)
                                       . QC/
                                                                           - .0004
                                       ,000 !
                                      . Ooo/
                                    , ooo
0003
                                   . oo 06
                                    •oo/i
                                     OO
             NET WATER
             (ml = gm)
                                            42

-------
                           CASCADE IMPACTOR RESULTS


Client:  ฃ PA


Sampling Location:    A l/CGft


Date:  S3  A


Run No:  / 7
               Dp (ปDpc),     Particulate         Weight %        Cumulative %
ITEM           microns        collected, me	collected	less than Dp
Cyclone


Stage #1        ^


Stage #2        2.


Stage #3       /. -772.          ^- 1


Stage #4      O. 93 <2          O.  3


Stage #5       0.3-92.          ฐ* ^            x^. 3           -2^,^


Filter           •                                   ^"^

-------
KEUFFEL a ESSER CO.  MADE In USA
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-------
                              CASCADE  IMPACTOR DATA
Client
Sampling  Location  A VER A&ET  f=*ffiEPl- At

Date   A O  Aes&c* *>T    /9"7*T"
Run Number
Comments
PARTICULATE
Cyclone

Stage #1

Stage #2

Stage #3

Stage #4

Stage #5

Filter (

TOTALS

MOISTORE
Bubbler  (#1)

Impinger  (#2)

Bubbler  (,#3)

Bubbler  (#4)

TOTALS
 FINAL
  (gm)

- ^ T / 7
                                               TARE
                                               (gm)
                   - 2-2-
             - / ?/  . 2.
                               FINAL
                                (gm)
                TARE
                (ga)
 NET PARTICULATE
       (gซn)

    . .C3 o i 2.

 _  _• O PO "2-

  / O 00 /	

  ,  o oo'3	

  .OOP/	

. OOP/	
                                  ,002*1
NET WATER
(ml ป gm)
                                                 45

-------
                           CASCADE  LMPACTOR RESULTS
Client:
Sampling Location:
Date:
Run No:   2.
                                 /*//?ฃ/* 'X >?<: ^r
ITEM
               Dp  (=Dpc),
               microns
               Particulate
               collected, mg
Weight %
collected
 Cumulative %
less than Dp
Cyclone


Stage #1


Stage #2


Stage #3


Stage #4


Stage #5


Filter
2. 9ฃ 9


2.03Q


/. 090
                                  ; . 3.
                                    .  /

                                    ,9
                                                   /O.3.

-------
                      99.9 99.
 90       80     70    60    50   40
                                     20        10      5
                       1    0.5    0.2  0.1 0.05    0.01
                                                                                                                                                                              ,10
                                                                                                                                                                               9
                                                                                                                                                                               8
                                                                                                                                                                               7
Vป
5   '.-
         0.01   0.05 0.1  0.2    0.5    1     2
10
20     30    40    50   60    70     80
90      95       98    99
                                                                                           99.8 99.9       99.99

-------
                              APPENDIX H
                    Velocity Correction Coefficient
The reference point velocity correction calculation was performed on 3 of the n
variable samples.  Findings are discussed on Page 8.  The procedures, for weasur
and cal culatiRปApfe--fet*ซA iir-l^-frvw^iire" seption 3 Page 13,
                                                         ft
OF

-------
JOB NAME
            VALENTINE, FISHER & TOMLINSON  • CONSULTING ENGINEERS
                              COMPUTATION & DESIGNING SMCET

                                                                 '   -  2. ฃ"" -
PREPARED BY.

SUBJECT	ฃ1
                                                           PAGE.
                                                                        OF
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-------
             VALENTINE, FISHER &TOML1NSON  • CONSULTING  ENGINEERS
                                COMPUTATION & DESIGNING SHEET
JOB NAME
PREPARED BY



SUSJECT__
                                                              DATE-



                                                              PAGE-
                                                                            - 7sr
                                                                          -OF_

-------
                                      APPENDIX  I
                                  Wood Burning  Rates
        The wood burning rate data was collected during each  POM  and  particulate emission
        evaluation.  The data was collected by  the methods described  in  the  Procedure
        section, Page 16.
                                                                                 •- ~3
                                        / 2L
_„.ฃ	
                                        4.
', &ฃ.
                                                             
-------
                              APPENDIX J

                  Auxiliary Atmospheric Emission Data
Two projects separate to this study were performed by Valentine, Fisher  &
Tomlinson wherein atmospheric emissions were measured from  combustion  of fuels
in residential fireplaces.  The first project was evaluating  emissions from a
compacted-waste-wood formed into a log and burned under  simulated  fireplace
conditions.  The results of the emissions are shown in Table  VI.   The
second project was sampling atmospheric emissions from burning  alder wood  in a
residential fireplace and were reported in a paper by W. D. Snowden .and
I. J. Primlani titled "Atmospheric Emissions from Residential Space Heating,"
presented at the Pacific Northwest International Section of the Air Pollution
Control Association annual meeting in Boise, Idaho, in November, 1974.   Emissions
from the second project are also shown in Table VI.
                               Table VI

             Auxiliary  Fireplace Atmospheric  Emission Data
Project
  No.

   1

   2

   3*
Burning Rate
    (BR)

  8 kg/hr

19.8 kg/hr

7258 kg/hr
Stack
Temp.

 54ฐ C

107ฐ C

363ฐ C
Stack Gas
Flow Rate

14.2 m3/min

11.7 m3/min

3881 m3/min
Pollutant
Mass Rate(PMR)  %CO
18.8 gm/hr

129 gm/hr

34500 gm/hr
      (PMR/BR)

0.2%  2.4 gm/kg

0.25% 6.5 gm/kg

3.5%  4.8 gm/kg
 *Air  Curtain Wood Waste Combustion System
                                              52

-------
APPENDIX K, COMPUTER PRINT-OUTS OF PARTICULATE EMISSION  DATA
WITH CALCULATIONS AND TERMINOLOGY
                                        53

-------
      PARTICULATE CONCENTRATION AND PMR CALCULATION TERMINOLOGY

VOLm      = Dry gas meter volume @ meter temperature and pressure, dry - acf

Pm        ป Dry gas meter pressure (recorded as inlet deflection accross orifjj
            meter) - "Hg
          = Dry gas meter temperature (average of inlet and outlet)

PSTD      = Standard atmospheric pressure (29.92" Hg)

TSTD      * Standard Temperature  (520 or 530ฐ R)

VOLW      * Volume of water collected (expressed as vapor at standard temperaq
            and pressure) - scf

M         = % water, calculated from amount the train collected in impinger,
            bubblers, and on silica gel

MF        ป Mole fraction of dry gas

WD        * Molecular weight of dry stack gas - Ib/lb mole

Wy        " Molecular weight of wet stack gas - Ib/lb mole

Wa        ป Molecular weight of air - Ib/lb mole

Cjj        ป Velocity correction coefficient for gas density

PSN      * Stack pressure  (static + barometric) - "Hg

C g       ป Velocity correction coefficient for stack pressure

VH^      ป Pitot tube pressure differential - "H^

V0        ป Stack velocity @ stack conditions - fps

Qo        ป Stack flow rate at stack conditions - acfm

Ts        ป Average stack temperature - *R

QQS      * Stack flow rate at standard conditions - scfm

T         - Time over which sample was collected - minutes

Vn        - Velocity of gases inside nozzle during sampling - fps

I         - % isokinetic (+ 10% desirable)

GO        - Particulate concentration - grains/scf

K         - % CO 2 by volume in stack  (12  indicate a no Z C02 correction  is  to
            be  made)

-------
      PARTICULATE CONCENTRATION AND PMR CALCULATION TERMINOLOGY



          = Particulate concentration corrected  to 12% COj

          * Pollutant mass rate - "concentration method" -  Ib/hr

PMR.,.     = Pollutant mass rate - "area ratio method" - Ib/hr

PMRAVQ    ป Average pollutant mass rate - Ib/hr

C         = Particulate concentration corrected for non-isokinetic sampling
            condition-grains/scf

P-p        ป Total Particulate collected by sampling train - mg

AS        = Area of Stack -

A         a Area of Nozzle -
VH        ซ Velocity head readings for pitot tube - inches water

VOLSTD    ™  Standardized gas that passed through the sampling train -
             cubic feet, 70* F.,  1 atmosphere pressure, and dry.

Cp        =  Velocity correction  coefficient for type pitot tube - dimensionless
             0,83 to 0.87 for "S" type pitot tube normally and 1.0 for "P"
             type pitot tube.
                                                55

-------
            PARTICULATE  CONCENTRATION & PMR CALCULATIONS
1.    VOL
         STD
                 (VOLJ  (Pm)  (TSTD)
2.    M
3.    MF
4.
5.    CT
(100)  (VOLy)
VOLg-jj) + VOLw


 100 - M
    100


(WD)  (MF) + 18 (1-MF)
                    Wa*
                                           15.
                                            16.
                                      -  (C0)  (QOS)  (0.008571)
                                                          -7-7—  (0.000132)
                                                           t   ftn
                                            17.   PMRAVG **
18.  C

*    PSTD
*    w_
                                                           PMR,
                                                              'AVG
                                                                   (1400)
                                                           QOSN
                                                           29.92" Hg.
                                                           28.95 LB/LB MOLE
                    •SN
7.    K
8.    Vr
                   2.9 (Ka) (C) (CD)  (Cs)
9.
                   (V0)  (As)  (60)
10.
11.   V
12.    I
13.    C,
 14.    C
                      (TS)
                  (VOLSTD) (PSTD)(TS)
                  (MF)  (TSTD)  (PSN) (T) (%) (60)

                  (100) .*
                         o
                   PT
                 ,,,ซ	 (0.0154)
                 VOLSTD

                 C0  (12%)
                     N
                                               56

-------
CALCULATIONS (Continued)

The weight of the dust per volume and weight of dust per  time were  calculated
using two procedures:

1.   The Concentration Method:

     The concentration of dust entering the sampling nozzle  is  calculated  and
     then multiplied by the volumetric flow rate of the stack gases  to
     obtain the Pollutant Mass Rate  (PMR).

     Concentration in Nozzle x Volumetric Flow Rate = Pollutant Mass Rate
                                                      On  Concentration  Basis.

           (l'T/VOL(;TD) x QQS = PMRp

Assuming the nozzle velocity is greater than the average  stack  gas  velocity
 (V  greater than V ), the calculated Pollutant Mass Rate  will be  less than
 the true Pollutant Mass Rate because the heavier dust particles will leave
 their streamline and not enter the nozzle.  If VR is less than  V  then  the
 calculated  PMR will be greater than  the true PMR.

 2.   The Area Ratio Method:

     The weight of dust collected is divided by the sampling time and
     multiplied by the ratio of the  Stack Area to the nozzle area to
     obtain the calculated Pollutant Mass Rate (PMRAR).

     Weight Collected         Area of Stack        Pollutant Mass Rate
     Sample Time          X   Area of Nozzle    =  on Area Ratio  Basis.

     (PT/T) x Ag/An - PMRAR

Assuming the nozzle velocity is greater than the average  stack  gas  velocity
 (Vn greater than V0), the calculated Pollutant Mass Rate  will be  greater
 than the true Pollutant Mass Rate because the lighter particles in  the  dust
 laden stream follow their streamlines and enter the sampling nozzle resulting
 in P /T being greater than  true.  If VQ is less than VQ,  the calculated
PMRAR wil1 be 8reater than the true  PMR.

To obtain  a more true Pollutant Mass Rate, the two calculated pollutant mass
 rates are  averaged.  This allows some of  the bias introduced because of
non-isokinetic sampling calculated by one method to offset the  bias of  the
other method.

-------
VALENTINE, FISHER & TOMLINSON /

CONSULTING ENGINEERS       / COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DA
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-------
S/ALENTINE, FISHER & TOMLINSON /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
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-------
VALENTINE, FISHER &TOMLINSON  /
CONSULTING ENGINEERS        /  COMPUTER PR I NT-OUT OF ATMOSPHERIC EMISSION DAI
BOCBADCTt BV *S W^ fV-SG /VX APPPOVFn

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-------
VALENT!NE, FISHER & TOMLINSON
CONSULTING ENGINEERS
COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
)B NAME '•' — ' ' • 	 '•+*-' -m-i-m !••,,.
rcr^ner QV •StomSi'ฃ0S\r *ปปtnvi

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29-84 pm 66ฐ T*
530 Tป™d 1-816590
532 Tซ
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15-321948 YOLstd 6 9 ฐ" Tป
2-274862
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0 • 0075

2-620800 700
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2-291287
0-9.73792
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710
25-614332 Ww 3-263433

1-005847 c O.QI
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1-C01843 Cj
0 -01
745
2-729468

0 • 02
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3 • 883297

0-02
735
3-834057

C • 0075
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0 • 0075
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0-0125
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2-947456
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C-015 VH
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3 -22S776
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-------
VALENTINE, FISHER & TOMLINSON /
CONSULTING ENGINEERS         /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION Di
JOB NAME
PREPARED BY-

SUBJECT—^
                                                       DATE
Pm
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VOLw
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-------
/ALENTINE, FISHER & TOMLINSON /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
DB NAME -*•ซ*-*=ป — ซ— TTป^. . •ปซ- .-••ป• 	
	 _.„ซ.„ DV ^44/V) /f^S 0/^ Aปป*nv
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29.307 VOLm C-015 VH
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530 Tstd " <"1'c<:

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2S.Bc7r<3 VOL.td ,.146"ฐ T'

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28-89 *** ฐ'015
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28 -672S53 w 3 ' 1 3 4 4 8 5
1-004820 c. ฐ'01
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0-988503 f
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667
3 • 163068

0 -0125
660
2-872281
0-015
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3-146426

0-01
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0-015
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3-217141

0 • 027
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JA/ A/a. &
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700 TS
3-741657

0- 075 VH
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7- 035623

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0-015
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3- 193743
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3-660601

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-------
VALENTINE, FISHERY TQMLIN5ON /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DAT!
JOB NAME
SUBJECT.
              VOLm
 - ' '_ c• ฐ  Pm
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3166-3  VOLstd

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-------
VALENTINE, FISHER & TOMLINSON
CONSULTING  ENGINEERS
COMPUTER PRINT-OUTCF ATMOSPHERIC EMISSION DATA
FrtEfปARED BY 'StlfAA/gG/r APPIOVFO

32-059 vOLm C-012 VH
29-61 635 Ts
c T ซ Pm 2-760434
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0-01 VH
29-656479 VOLstd 62ฐ Ts
2-489979
0 ' 5 9 VOLw
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1-950600 M 62ฐ
2 -489979
C-980494 MF
28-88 Wd C-015
650
28-667774 Ww 3-122496
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29*55 .Psn 2.4S9979
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1-006241^5 o>oi5
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3- 170173

0 • 0175
650
3 • 372684

C • 020
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3-605551
0-012
700
2 • 898275

C-015
690
3- 217141

0-020
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3 -591656



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C-015 VH
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3-074085
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3 • 228776
0-0175
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3 • 424178
0-0175
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3-424178
0-022
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3-882009

0- 01
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0-0125
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0-0175
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3-097340
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7-683198
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-------
VALENTINE, FISHER & TOMLINSON  /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION D|
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-------
VALEN"NE, FISHER & TOMLINSON
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
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31-515051 vOLstd 665 Ts
vwi3Ta 2.S24889
C-72C4S VQLw
0-015
2-23500 0 M 67ฐ
3- 170173
0-977650 MB
J8.=8 ฃ 0-03
690
2 S • 6 3 6 3 3 2 Ww 3-714835
1-005452 Cd 0-0175
29-7 p$n 710
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1-003656 Cs
0-0125
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2-947456

0-0175
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3-424178
0-0175
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3-372684

0-01
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2 -598076

0-015
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3-217141

0-015
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3-286335




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3-646916

0-01 VH
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0-012
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3 -687817
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0-022
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-------
VALENTINE, FISHER & TOMLINSON  /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DA

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-------
'ALENTINE, FISHER & TOMLJNSON /
ONSULTING  ENGINEERS       /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA

Jeฐ/GEPL.Ae&~ & Mf^^JAMS,
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2 -653299

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3 • 096366
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2- 537715
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-------
VALENTINE, FISHER &TOMUNSON  .
CONSULTING ENGINEERS         /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DA
JOB NAME
        ฃT.X>A.  fr/tpe&LA^E.
                                                       DATE
                                             X AV&* /Q-7f
PREPARED BY-

SUBJECT-
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Pm
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VO4.W
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-------
IALENTINE, FISHER &TOMLINSON  /
INSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
jB NAM6. — • - i-i ir. 	 —
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?5-503 VOLm
L. ' >' * c ? Pm
5 3 c T std
541 Tm
21,- 79 23 9 5 VOL std
0-69673 VQLw

2-733600 M
C-972664 Mp
25-85 Wd
28ซ5ฃ2584 yyw
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25 '65 Psn
1-004542 Cs

























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0-005 VH
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1-739252
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1-767766

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C • 012
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0-013
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3-274141

0 • 0 0 8
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2-323790

0-014
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3-051229

0-014
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3 • 146^26
0-01 VH
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2-653299
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-------
JOB NAME
         Z'&A. ;=•/#ฃ pi_
        COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DA7
                                   ^.2  Ats&US.'T  23-K-
PREPARED BY
SUBJECT-
                                                        DATE.
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       25 ' 7 -   Pm
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-------
VALENTINE, FISHER & TOMLINSON /
CONSULTING  ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
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-------
VALENTINE, FISHER & TOMLINSON
CONSULTING ENGINEERS
COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DAI
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-------
COMPUTER PRIMT-OUT OF ATMOSPHERIC EMISSION DATA
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-------
VALENTINE, FISHER & TOMLINSON
CONSULTING  ENGINEERS
JOB NAME
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-------
COMPUTER PRIMT-OUTOFATMOSPHERIC EIUSS.ON DATA
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-------
VALENTINE, FISHER & TOMLINSON
CONSULTING ENGINEERS
JOB NAME
      COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
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-------
ALENTINE, FISHER & TOMLINSON
ONSULTING ENGINEERS          COMPUTER PRINT-OUT Of ATMOSPHERIC EMISSION DATA
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-------
VALENTINE, FISHER & TOMLINSON
CONSULTING  ENGINEERS

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-------
/ALENTINE, FISHER & TOMLINSON  /
CONSULTING ENGINEERS        /  COMPUTER PRINT-OUT OF ATMOSPHERIC EMISSION DATA
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-------
                              APPENDIX L

                              Data Sheets
This appendix contains Field Data Sheets with corresponding Moisture Determination
Sheet, Laboratory Analysis and Total Particulate Sheet, and Oreat Data and
Calculation Sheet for all particulate and POM samples.  Field Data and Moisture
Determination Sheets for the particle sizing runs are included also.

Pages are ordered by run number.

PARTICULATE SAMPLES           RUN NO.                       PAGE NO.
     Alder                    1, 2, 3, 4                     83-98
     Douglas Fir              7, 8, 9, 10                   106-121
     Coal                     12, 13                        126-133
     Locust                   14, 15, 16, 18                134-145, 148-151
     Pine                     19, 20, 22  (Glass Front), 23 152-159, 163-170


IMPACTOR SAMPLES              RUN NO.                       PAGE NO.
     Alder                    5                              99-100
     Locust                   17                            146-147
     Pine                     24                            171-172
POM SAMPLES                   RUN NO.                       PAGE NO.
     Alder                    6                             101-105
     Douglas Fir              11                            122-125
     Pine                     21                            160-162

-------
00
Co
                                     sic
                             /' .1^
PORT
DATE
OPERATOR/5
RUN NO.
METER BOX AH
FILTER NO. 2-"? -5  g TARF  */^
                                                      VALENTINE FISHCt A TOMLINSON
                                                           SEATTLE. WASHINGTON
                                                          TRAVERSE SAMPLING DATA SHEET
                                                         IMPORTANT:  FILL IN  ALL BLANKS
                                                                          <-a. (>
                                                                                                                    64-
BAROMETRIC PRESSURE (PB).
AMBIENT rmmiTMiKr \,s,-<.t.
PORT PRESSURE (Ps)_:2ili."H20 •
                                                                                                                                               _"Hg
                                                                                                                                                'Hg
                                                                                                                                                "Hg
                                                                                                    ASSUMED MOISTURE
                                                                                                    C
                                                                                                    REF.AR
       SAMPLE t METER BOX NUMBERSXS^Iป
                          •& ? 7
                                                                                                            STACK DIMENSIONS
PROBE NOZZLEIA.
PROBE
       CLEAN-UP NO.
       BOX A PROBE HEATER SETTING_2lฃii
                                                       SCHEMATIC OF TRAV
                                                                         SE POINT LAYOUT

-------
                          VALENTINE,  FISHER &  TOMLINSON
                    STACK MOISTURE CONTENT DATA AND  CALCULATIONS
                                                 64-5
CLIENT    A
ฃ-/ฃฃ
                           *>'_ M
-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE  SHEET


CLIENT   ฃ"Pซq /Zrฃjฃs^4<-ฃ.	 DATE OF ANALYSIS  7 -2.f- ~l
EVALUATION LOCATION   Ai-'??A<=.ซ'   /^/eS ฃ*.r\Cf.	 RUN NO.   /

EVALUATION DATE   1 -~L <=) . -> &T	 CLEAN-UP  SET NO.     (=>
I.   EVAPORATION  OF       Q	(ml) OF
     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL  77^06-/(me) - TARE   77 3JS, g      (mg)

          -BLANK ((  >:COS?  mg/ml) (   9 O     ml) =  .5"  mg)            'j,

II.  FILTER CATCH   /V?jT/4  //O6   2,       (mg)

           -BLANK (         //^       mg)

 IV.   PARTICULATE FROM EVAPORATION OF    2 / Q _ (ml)  WATER
      IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
           FINAL ~?g2 H'n (mg) - TARE   ^6 ; 32 V. 8       (mg)

           -BLANK ((  , 'H    mg/ml)  (     2./O _ ml initial

           -     / Q."L  ml CONDENSED -  1 ^^ >B ml)  =  ^4   mg)   =  JJ -3

 V.    PARTICULATE FROM /^C"    (ml) OF fce. /r-r* +, r-   RINSE  OF IMPINGER,
      BUBBLERS, AND CONNECTORS AFTER FILTER:

           FINAL 77^0 /. /  (mg) - TARE 7? 3 Q 4T . 7 _ (mg)

           -BLANK ft.OQg?  mg/ml)  (  / TsT    ml) =   •?    mg)        -   /^ ^   .

 VI.  TOTAL PARTICULATE -  I 4-  II +  III + IV + V                      -   /g> 3 .^3^

      BLANKS
      -                                                     FINAL  73 *T2 'o-i
      ACETONE =    . B      mg/_/4O__ml  -  .OO^I   mg/ml    TARE  r?^ ซ• "2 a"- j.

      ETHER-CHLOROFORM =     // ^      mg. (FINAL 7 ^ 2. 8Ot7m%  -   TARE  7^ "-TjP,?_
      WATER =     / ^ _ mg/   /-/ -ฐ  ml  =  / 0^3.     mg/ml.  FINAL
                                                                 TARE
                                             85

-------
                     VALENTINE,  FISHER &  TOMLINSON
                   ORSAT DATA  AND  CALCULATION  SHEET
CLIENT
SAMPLING POINT
DATE 7/ZB//
/
TIME OF SAMPLE
CUliULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100-Above)

LOCATION d^/^/s*
'ฃ"" RUN NO. ฃ//&
COLLECTION 2-'3Q~33
ANALYSIS ANALYSIS
#1 #2
C- / ' <ฃ>• O
ซT- /,0 \ -2', 0
*/.o *'.<*
\
\


#1 #2
, 1 0
70,*? 2. /,o
O O

1
i

^n ^) 1 O ^^ *ซ*~ป

v-^v ^l/rzAT- ^^x^ ^^j>c/rr
HOW COLLECTED &ฃ*?-'$ J^i*
/ , f' /
'O^/r^IME OF ANALYSIS ^'^ ^/^^/^"
ANALYSIS ANALYSIS
#3 #4

.2 /.O !
-2/. c?


i ~" j

RATIO \WT./MOLE
#3 #4 AVG. j MOLE WT\ (DRY)
! i
,| , 0 l-Tt 44/100 ,0!*}
) '
7^.9 3Qt7 32/100 •(Ql(0\<\
'O 2S/100 O
! i I
i
!

'^' ' 7?'0fe7 28/100 2?J2?
AVG. MOLECULAR 2.3-78
                                                  WT.  DRY  STACK GAS

-------
..j^.
X>7, f-)
65-5
CLIENT/" /v/' /""//'/- /^/.xy<-/"
PORT LOCATI
DATE • 2 •-'
OPERATOR/S
RUN NO.
SAMPLE & ME
METER BOX I
FILTER NO.^
CLEAN-UP NO
BOX & PROBE
/
ON <-'(', -\//'*t S X/S'~At^>'/') /\J ::>;; \_-' /} ^f< '']/< /J

TER BOX NUK
iH // /(
IBFBS<^^i
*'•) 7
l~* ~ ^ 9 TARE •ฃ/_/ 
d />'
IMPORTANT: FJU IซjซLl BUWKS PORT PRESSI
x x w."*^ PCU " PH "^
^i> -rfr/ /• / / j y/ • ' jn
4 v " X ^ (" T*-^- ASSUMED MO
(^ ^/A- "V/^ '^ ' j t C FACTOR
PO)'-'^" "H9
/•v >'/ x/--, /

IBF (P3) - 7 / , "H20 - "Hg
PS .-'>&.? ^T~ "He
I1TI1RF -^ ' I
• a 5^"
.'^"y^' , y.' REF.AP >•)? - •?', '~.'.'-i>T? u-y?
jป- " C> 1*Jj'*'i>">* STACK DIMENSION^!^
V ' l/ฃ :~ / R ' ,vy PROBE NOZZLE DIA.^L-!
SCHEMATIC OF TRAVERSE *ป01NT IIIYOUT^ * PROBE LENGTH '^
INSTANTANEOUS READINGS: RECORDED 0 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
/ *;- -f,_j
/ *>" 5 "-5
' 1>~ 3(s>
/ •-/.•:• X/-y
'77^
y 'i -S ?/

•'d-^2.
/',,,;> s"
• >
/tC^ ^ i_
,63*-

TOTAL /
AVERAGE
ELAP.
TIME
(MIN)
O
,-}
(.

/ -3— '

.9 7.....
- > -
-^L •
~~'-j^~
'-,,
% v -
- • —
&0
V-//S
DRY GAS METER
(CUBIC FEET)

. Jv. :V/ 1>
6~ J-t -*f~ ^
c!TZ! vVy
/"vi'i/
&'/jbT'->7y

-27 .3"^^
7//////
DRY GAS TEMP.
INLET
7rt
(9<- )
3 (.,<->
j?y\>
.? /.ปo>
^5~J
s
^r
S|
	
/ / /
///,
1MP1NGER
TEMP.
t'F)
-3f.y
*& 1
•y. -^
•& -f-
"f •4-
-}(.,
y ^
^5-,.^
s ^
S f .>
'j '(. >
b /
i/fc
lฃ.
	 	


^''AREA /J ?<> fi
'/IN; AN./..)fA/.? - ;
' - 2
/•> -^
i.
i
/•
^
> "^ .
'^1 /
- .... ^
i_^d


-7T-S.,
J2^?
'///

PITOT VH
, ^ /
- r9/ K-"

' J / ^ S"
x/*5"
4.jy ••. ••
^.^ 7^
-. <>x?
, .y /
ซ •>/
nซJ/.\
- J/S
.. • y /
. y/ ซ•, -
- -> / -^
.. *'2..
*J.t j~"


- - - -


. /" -4.' - >^ > . .
V///,

ORIFICE AH
("H20)
DESIRED
. ^-.f-
*<> d
s c-^.
w ^//',
../,ฃ,
-v <;- ^
.. 7f>
. ^ j
.ป -/?
.(..y
.j f" ./
"i^ir
..-/'>
-^ ^
T^5 "
--- --•


' j-r . ,r
Y//;
ACTUAL
//"/•/
* ~^'~*ii
-c-' •—
. 
. f'r. C-
:. '/O
. X 'h
T0~"
^ c. /
- f/ >
•• i/i/*
- C-:/
- 1 • .y
- -^"H2ฐ •.Ui 5'"9
Prt - PB *AH * .3V.X .1'. ,) "Hg
PUMP
VACUUM
("HgGA)

-> O
-?. /
/, -
,-', ,)
-V. 't
?,>:j
j?^ j
/, V
/, 'j.
X*. ^
— ' ' t
/. •,
:> *')
j • )
•j S"
/ u

^tr-



f S f j
// /
•'///..

STACK
TEMP.
(•F)
.2,*,,
~J-f <*>
-y 1' >
•?/,•>-
-i' r> .O
-' •"> O
- J ^> -J
..-•' -<• /
.V/ ^
^ / %
t
> /'.y
J* <1 v





^S2L
Z^6
6tf6'ft
OPACITY
OR
ZC02


,^ AY
/, j_j .

— ปi.


-^•*-

ป-ป'^ '
•'



,.<•/•—.--' y
,. X
•ป ' • . /






x /



}
fi
r.
                  // /
               , J/i)
                <.*'.>

-------
                          VALENTINE, FISHER  & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND  CALCULATIONS
CLIENT
            -
           /-
LOCATION

OPERATOR
                      O /V
                                 ••> <-
                                                             RUN  NO.
DATE
                                                                      NO.J
                                                                       25 /
SAMPLE BOX
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                           3? 7.
                                           6
                                                             INITIAL
                                                         447.0"
                                                                      o.
H20 CONDENSED, ml (1 ml = 1 gm)
     BUBBLER (#1 W/APPROX.  100 ml  WATER)

     IMPINGER (#2 W/APPROX.  100 ml WATER)

     BUBBLER (#3 DRY)

H20 ABSORBED BY  SILICA GEL, ml
 TOTAL H20 COLLECTED, ml
 VOL. OF H20 VAPOR @  708F. AND 1 ATM.
 0.0474 x TOTAL H2Q


 MOISTURE IN STACK GAS,  %


 MOLE FRACTION OF DRY GAS


 MOLECULAR  WT. OF STACK  GAS
 I MOISTURE IN  STACK GAS  -  100  x VOL.  H2Q VAPOR
                            VOL.  DRY GAS + VOL. WET GAS
 MOLE FRACTION OF  DRY  GAS  - l.QO-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT.  OF STACK GAS - AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION 't-
                              is X  (1-MOLE FRACTION)
          NET
          3.5—
                                                                       /.  -7-
          7.7
VFT/AP3C
                                           88

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY  ANALYSIS AND TOTAL PARTICULATE  SHEET
                       'Pi.ฃCE-	 DATE OF ANALYSIS ~7-2.<=* -'

EVALUATION LOCATION   A I/El/?/6, ฃ~   /^/^/T,ฐ4-/^C .f	 RUN NO.       Z-

EVALUATION DATE    "7- 2. *9 -75  '	 CLEAN-UP SET NO.
I.   EVAPORATION OF    /^*5"     (ml) OF   /) C ฃ" 7"C? /*/ ฃ-—

     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE  BEFORE
     FILTER.

          FINAL 78g^3.Z(mg) - TARE   7<5> ~ TARE   -7^^-4~S~^      (mg)

          -BLANK (     /• 8 _ mg)                           =    7.
IV.   PARTICULATE FROM EVAPORATION OF     2L 9 0    (ml)  WATER
      IN  IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
           FINAL ~?~)^J 83 (mg) - TARE   775*^0.6      (mg)

           -BLANK ((.Q02gฃ mg/ml)  (    2. ^Q _ ml initial

                         ml CONDENSED -  ^?^ป Co  ml)  - 0. 
-------
                    VALENTINE, FISHER & TOMLINSON
                  ORSAT DATA AND CALCULATION SHEET
CLIENT _

SAMPLING POINT LOCATION

OATH 7-29-7S"     RUN  NO.  7^/o
                                        HOW COLLECTED
TIME OF SAMPLE COLLECTION
                                        TIME OF ANALYSIS
CUMULATIVE
% 3Y VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100 -Above)

ANALYSIS
//I
o,l
20,8
to. 3




#1
o 7
2.0. ^
O



' ' ฃ-

ANALYSIS
#2
0,<ฃ
?o,7
20,8




n

2o//
. I



7^2,

ANALYSIS ANALYSIS
#3 #4
^ ^ '
.
I
?o,7
i
i


| RATIO \WT./MOLE
#3 #4 I AVG. MOLE WT\ (DRY)
! l
<9, 6 ' -^^ 44/100 ,2/7?
i 1
2O, / 2-<2- 1 32/100 ฃ,4? 2
o :. z>33 2a/ioo -^o^
, j i
i

' ^ I
"^ '^ 7f.2?^| 28/100 2-ป ASS"
AVG. MOLECULAR 2
-------
              / w A'
                                                                                                 66-5
ri IFMT

PORT
OPFRATQH/S.

ftUN NO.   .
                      ' i- - /v/ / / l/
                                                     VAIENTINI  FISHIR ซ TOMUNSOM
                                                          SEATTll. WASHINGTON

                                                        TRAVERSE  SAMPLING DATA SHEET
                                                        IMPORTANT:  FILL IN ALL BLANKS

                                                     b'/^.  /v //  .0 / 7 "—
SAMPLE I METER BOX
METER BOX AH   /  -/ ,'V ") 1	

FILTER MQ.go-^  ^TARE */ R 3.O
                                                                             BAROMETRIC PRESSURE (PB)

                                                                             AMBIENT CONOITIONS.fjL

                                                                             PORT PRESSURE (PS)- /  ) "H20

                                                                             PSN " PB + PS	.
                                                                             ASSUMED MOISTURE.
                                                                             C FACTOR   ••>••>"•.

                                                                             REF.AP	u_
                                                                                                                          ->-:>   '  S
                                                                                                   _"Hg
                                                                                                   ."Hq

                                                                                                   -•Hq
                                                                                                   _Jt
                 ; BLANKS.
CLEAN-UP NO.

BOX &  PROBE HEATER SETTING JLฑiฃ_ &.
>'-0

                                                      SCHEMATIC OF TRAVERSE POINT LAYOUT
                                                                             STACK DIMtMS IOMs3 -y* H^ AREA /*/ / ?&  f2

                                                                             PROBE NOZZLE DIA.fijฃlN; AN -g^/36 p2

                                                                             PROBE LENGTH	FT	IN.
  INSTANTANEOUS READINGS:  RECORDED • BEGINNING OF TIME INTERVAL
                                                                        AVERAGE VALUES READ WITHIN THE TIME INTERVAL
   CLOCK
   TIME
 (24 HRS)
            ELAP.
            TIME
            (MIN)
DRY GAS METER

(CUBIC FEET)
   DRY
TEMP.
  INLET
OUTLET
BOX
TEMP.
CF)
IMPINGER
  TEMP.
  CF)
POINT    PITOT VH
  ORIFICE
E  AH
HzOJ
 DESIRED
f f  ' s
   ACTUAL
  > /  / ,
 PUMP
 VACUUM
("Hq 6A)
/ /  / /
STACK
TEMP.
CF)
                                                                                                                      J  / J  .'
OPACITY
  OR
 ZC02
                                                                                                                                    ~m
              u  4
 / 7
J..7^LZ.
 I'^y'}
/ 7//
/^Z-
 /_7_^
  7xf^
  7->  /
/ 77-1
      ซ;•
       ' >
                        ~7 .
                                                                      ฃ=
                           .  //
                                                                               ^ <_.>.•>  >
                                                                                                                       /7V
    V*   ^*? "7
   'JL^lAS.
                                                                                 ,">.-•> 7
                                             _9-i
                   ^/^~
                ^.9
                                                                                                             -^  ,9
                    6'
                              7
                                                -/
                                                                      /> -
                                                                                                                                           00 /
                                                                                                                                         ..-)*!/
                    iii^C^iLlL'.
                    /.. s'^. >?/s^
                                                                      D - J
               o*l ~)
                / /
            -A
                                                                           y

                                                                                                                        K--S"
                        >-. ซ.-
                                   -*2-

                                                                      1--  ^
                                                                                                             f. o
                                                                                                                                          OO /
                                                                                           . 'J
                                                                                                             /, O
                                                                           2
                                                                                           -< .-?.
                                                                                                             /  ft
                                                                                                             s.o
                                                                                                                                - 3
                                                                                                            Zi_i2_
                                                                                                            '/. o
                                                                                                            /  s / /
 TOTAL'
                                                                      777,
                                                                                            3/'M20 -,<

-------
                          VALENTINE, FISHER  & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND'CALCULATIONS
CLIENT
                                                             RUN NO.
LOCATION

OPERATOR
                                                                      NO.
                                                             DATE  7/7 S /7s
SAMPLE BOX
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                                 ', S
                                                             INITIAL
H2u CONDENSED, ml (1 ml = 1 gm)
     BUBBLER (//I  W/APPROX.  100 ml  WATER)

     IMPINGER (#2 W/APPROX.  100 ml WATER)

     BUBBLER (#3  DRY)
H20 ABSORBED BY SILICA GEL, ml
TOTAL H20 COLLECTED, ml
VOL. OF H20 VAPOR @ 70ฐF. AND 1 ATM.
0.0474 x TOTAL H->O
 MOISTURE  IN  STACK GAS,  %
 MOLE FRACTION OF  DRY GAS
 MOLECULAR WT. OF  STACK  GAS
 1  MOISTURE  IN  STACK GAS  =  100  x VOL.  H20  VAPOR
                            VOL.  DRY GAS + VOL. WET GAS
 MOLE FRACTION  OF  DRY  GAS  =  100-%  MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT.  OF STACK GAS  = AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION +
                              18 X  (1-MOLE FRACTION)
NET
                                                                      -3,
                                                                       iJ.  /
VFT7AP3C

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT ฃ1 r*A   Ft/???ฃ>ฃ-A Cฃ.	 DATE  OF ANALYSIS   7- 2^-7 ^~

EVALUATION LOCATION  A >S-T/*3 /i(^ฃ~ ฃ=//-?ฃ PL. + ; -jT	 RUN NO.     3	

EVALUATION DATE    ~7~2. ฐ) - 7J>	 CLEAN-UP SET NO.


I.   EVAPORATION OF     3<3	(ml) OF   A
     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL 7743/- -+ (mg) - TARE  7 7 ^ 2. &> .  2     (mg)

          -BLANK  ((.Q05-ฐ7  ma/ml) (  8 O    ml)  s   ^^  mg)

II.  FILTER CATCH     //Ob   /V S A	 (Media Type)
           FINAL <3-4-8~ 2.   (mg) - TARE   ^J5^. O	 (mg)      =  /5". "Z.

III. HYDROCARBON  OBTAINED BY AETHER-CHLOROFORM EXTRACTION ON        " 	    ^—
     WATER IN IMPINGER AND BUBBLERS.

           FINAL 77 * 9 7.^ (mg) - TARE  7 7 ^ 7 ^- 3	 (mg)

           -BLANK (     /. g	^Qg)                           =     /ซ 3
 IV.   PARTICULATE FROM EVAPORATION OF    2. •? O     (ml) WATER
      IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
           FINAL ?"??;?*.ฃ  (mg) - TARE  77*2. mg/ml)  (    ^- ^

ml) - C. 7 mg) V. PARTICULATE FROM ^ O (ml) OF Acฃro*/ฃ: RINSE OF IMPINGER, BUBBLERS, AND CONNECTORS AFTER FILTER: FINAL #ฃZ79. 7 (mg) - TARE ffg Z 73. ฃ (mg) -BLANK ((- ฐฐ5- 7 ing/ml) ( 7 ^ ml) - Q 5^ mg) - (a, 0 VI. TOTAL PARTICULATE - I + II + III + IV + V - 33 . (=> BLAI^KS _ , FINAL 7^5"3^. fa. ACETONE = ซ ^ mg/ /^^ ml ป . ^0,5" 7 mg/ml TARE 7 ^S~ 3 fT. g. ETHER-CHLOROFORM = /- 8 mg.(FINAL 7^2


-------
                     VALENTIN!-:,  FISHER & TOMLINSON
                   ORSAT  DATA  AND CALCULATION SHEET
CLIENT
SAMPLING POINT LOCATION   /*••'
            /V-SC/rVf/^;
DATE 2s) Jt/Sy /9-7JTRUN  NO.
TIME OF SA2-IPLE COLLECTION  / 7o3 -
             _ HOW COLLECTED 	

           ^  Til-IE OF ANALYSIS
CUiPJLATIVE     I ANALYSIS  :  ANALYSIS !  ANALYSIS j  ANALYSIS
7, BY VOL. (DRY)    //I          #2    \    -V/3    :     /M
               i O,/
0,0
o,/
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100-Above)
2O,'J ' ZO. 7
23, 7 ^o. 7
!

1
l
1

#1 : #2
i / 0,0
i
7to.fe 2o,7
0,0 0,0



19 -3 ! 7^-3
^,^ : j
7 : ^/100 ^62ฐl
1
20, s" i2o,4 32/100 ^,^?
1
fi.o ! O.o 2a/ioo ! o •
\ • '
! i i
, j
1 1
; ! ;
; i
9^'f ; 1^.333 28/100 \-27.1\i
                                                   AVG. MOLECULAR

                                                   WT. DRY  STACK GAS
                                                ฃ8-83
VT1/APA3

-------
           xrwr  <->/>   <-v   f"ซ:
CLIENT ฃ

PORT
DATE
                        /9 7b"
OPERATOR/ S .'
RUN NO.    -
                          A A? is
                                                    Ji _/
               VALENTINE FISHER A TOMLINSON
                    SEATTLE. WASHINOTON

                   TRAVERSE SAMPLING DATA SHEET
                  IMPORTANT:  FILL IN ALL BLANKS
                                               68-5
                                            BAROMETRIC PRESSURE
                                            AMBIENT CONOITIONSC
                                            PORT PRESSURE (PS)_
                                                                                                                                        "Hg
                                                                                                                          "M -
                                                                     _ฃ_"Hg
                                                                     	"Hg
SAMPLE* METER BOX NUMBERSฃฃV& _ /
METER BOX AH   A ^B^ 7

FILTER ซ.*?<
                                                                                                   ASSUMED MOISTURE.
                                                                                                   C FACTOR
                                                                                                              'j - /- " < •}, V
                                                      ,-;?
CLEAN-UP NO -- i  BLANKS _ ป

BOX & PROBE HEATER SETTING _ &
                                                              /•/ ^-
                                                                                    •*'
                                                      SCHEMATIC 'OF TRAVERSE POINT LAYOUT
                                                             STACK DIMฃNSIONS#MlM AREA
                                                             PROBE NOZZLE niA  V^2  IN: AN

                                                             PROBE LENGTH _-5__ FT
                                                                                                                                        f2

                                                                                                                                       . p2

                                                                                                                                        IN.
                                                                                                                                                 .• 2-
  INSTANTANEOUS READINGS:  RECORDED %  BEGINNING OF TIME INTERVAL
                                                                        AVERAGE VALUES READ WITHIN THE TIME INTERVAL
   CLOCK
   TIME
 (24 HRS)
            ELAP.
            TIME
            (MIN)
                     DRY GAS METER

                      (CUBIC FEET)
DRY GAS TEMP.
INLET     OUTLET
BOX
TEMP.
CF)
IMPINGER
  TEMP.
  CF)
POINT
PITOT VH

 ("HjO)
                                                        ORIFICE  AH
                                                      DESIRED
                              ACTUAL
PUMP
VACUUM
                                                                                                              y y y
 STACK
 TEMP.
 (*F)
y y / y
OPACITY
  OR
 XC02
                                                                                                                                 y  y y
/• ' / 7
7-y'yj/i-.
                                                                                      7~7
                                                                                           y  y y
                                    C,')
                                                                                      s-
                     /• /  ")  >J2 O
                     k (j^ - L* Q	
                                                                       4^2
                                                                                      Lil
                                                                                             -  -U'
                                                                                                               /x
                                                                       A
                                                                                                                 o
                                              <"• v,
           .. <
                           ._z_^_.
                     ^i^-3--L-
                                    ^7^-

                                                                                                     ^.V.:
                ZJ>
                /^
                ^o
                                             A^_
                        IUL
                                                                                             -.9
                                                                                                                        77s
                                                                                                                                             *••>
                                                                                                                          y s
                                    •-7/v
              )
                                              7..(2__

                                                                                                                                            .&/


                                                                                -••>/ s
                                                                                                                 0

                                                                                                                x  2.-
                                     5'J
                                            _T_S_:
                                             . Z.Z.
                                                       -? ^ <•>
                                                                                                                          s ' o
                                                                                - -> > 7S-
                                                                                                         0
                                                                  7
                                                                                                              /_2_
                                                                                                              /.  2
                                                                           /
 TOTAL' /
  '
                                                                       Z.&
                                                                                                  ,
/AVERAGE
                                                                                                                       237
                                                                               Pm - PB

-------
                          VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND  CALCULATIONS
CLIENT
                                                             RUN NO.
LOCATION

OPERATOR
                                                                      NO.
                       /
                                                             DATE  "? / jj / ?
SAMPLE BOX
H20 CONDENSED, ml  (1 ml - 1 gra)
     BUBULER (//I W/APPROX.  100  ml  WATER)

     IMPINGER (02 W/APPROX.  100 ml WATER)

     BUBBLER ($1 DRY)
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                                 .  2-
                                                             INITIAL
                                                           S6. (
H20 ABSORBED BY SILICA GEL, ml


TOTAL H20 COLLECTED, ml
 VOL. OF H20 VAPOR @  70 *F. AND  1 ATM.
 0.0474 x TOTAL H2o
 MOISTURE  IN  STACK GAS,  X
 MOLE  FRACTION  OF  DRY  GAS
 MOLECULAR WT.  OF  STACK GAS
 % MOISTURE IN STACK GAS  -  100 x VOL.  H2Q VAPOR
                            VOL.  DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS - 100-Z MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT.  OF STACK GAS - AVG.  DRY MOL.  WT. OF GAS X MOLE FRACTION +
                              18 X (1-MOLE FRACTION)
                                                                       NET
                                                                         L..7
                                                                         . o
                                                                         . /
VFT/AP3C

-------
                          VALENTINE, FISHER  &  TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ฃL^A   <-~/S~=*L^:ฃ   _ DATE OF ANALYSIS  7~3 G-~7

EVALUATION LOCATION A >/ฃT/ t=~  /^/Pl^PL. /? -I ^      RUN NO.
EVALUATION DATE    "7-30— 7_5—'	 CLEAN-UP SET NO.    6  g-


I.   EVAPORATION  OF    ^S^     (ml) OF   /?
     RINSE  &  BRUSHING OF NOZZLE, PROBE AND  GLASSWARE BEFORE
     FILTER.

          FINAL 72^2jฃ>fl(mg) - TARE   7 ~? // "7.6? _ (mg)

          -BLANK ((_-ฃฃjTj7_mg /ml)  (   ^-S""   ml)  = . .ฃ   mg )           ^ . ฃ     mg.

II.  FILTER CATCH  /*) '<, A  //&&  ฃ //      (Media Type)
           FINAL ^3?. ฃ    (mg) - TARE   ^2.^. C, _ (mg)      =   /3. 2.     mg.
       s>        /c?3> 8     *^>3 -        /3&- "2.           ~>3      -
 III. HYDROCARBON OBTAINED  BY ETHER-CHLOROFORM EXTRACTION ON
     WATER IN IMPINGER AND BUBBLERS.
           FINAL ^ ฃ"•?&/. '0  (mg)  -  TARE   ^^<*-4-OJ      (mg)

           -BLANK (    /. 8 _ mg)                            =   / 9. "7

 IV.   PARTICULATE FROM EVAPORATION OF   ^  / g2 _ (ml) WATER
      IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
           FINAL -7 •', ^^.-.Zdng)  -  TARE  7k 7ฃ ^-.^	  (mg)

           -BLANK C(_Lฃฃ2^^ mg/ml)  (  <2,/ ^	ml initial

           -    <^. 7    ml CONDENSED =• ^QA  ^  ml) ซ  - da  mg)    =    //. 2.    mg.

 V.    PARTICULATE FROM  BO   (ml)  OF ACฃ~T<2/Vฃ"  RINSE OF IMPINGER,
      BUBBLERS, AND CONNECTORS  AFTER FILTER:

           FINAL ~?8 28(*3- (mg) - TARE  7 S 2. 4-3 .^       (mg)

           -BLANK (( . a o.g- 7 mg/ml) (   g^    ml) -  > 4  mg)
 VI.  TOTAL PARTICULATE  =ป  I  + II + III + IV + V                      -  / & 6 .

      BLANKS
                                             _             FINAL
ACETONE -   . g _ mg/ /^^>  ml = _1_^Jฃ_7__mg/ml    TARE  7? r 3 ,T S

ETHER-CHLOROFORM  =     /.
                                g      mg. (FINAL 792gq7 mg -  TARE   7927^, 9  mg)
      WATER =    - ^       mg/ / ^ ml =  -OoZZv  mg/ml.  FINAL  "7v 9 7 3. -f
                                                                 TARE   7.0--' " ': . c:
 VFT/AP9 A


                                                97

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION  SHEET
CLIENT
SAMPLING POINT LOCATION	


DATE^A/A/ J<^' /^73'^RUN NO.
                                         HOW COLLECTED
                                                                    n •
TIME OF SAMPLE COLLECTION /6>'—- 7/^--  TIME OF ANALYSIS ^J L///. j /  /ฐl
                                                               '   7
CUMULATIVE
% BY VOL. (DRY)
C02
C02 •ป• 02
C02 •ป• Q2 + co




COMPOKENT
TL BT VOL. (DRY)
C02
02
CO



N7 (100-Abovc)
ANALYSIS
#1
<^7
-2o. <*
3o.^




#l
,7
\1.<\
OiO



79,^
ANALYSIS
#2
0~-5^
Z<3* ฃ
-?C?. ^




#2
x^'
ZOJ
o.o



7T-V
ANALYSIS
#3
ฃ.&
3&. L
20. (c




#3
, ^
20, O
oปo



75'V
ANALYSIS
M
a 7
40^
^C7,^




#4
/7
1^^
O, O



?T^


AVG.
,feZ*'
1?.??^
O,O



?T^

RATIO W./MOLE
MOLE WT\ (DRY)
44/100
32/100
24/100



28/100
AVG. MOLECULAR
,174T
6,^5^
O.Q



2?. ??2
2^>?0
                                                   WT.  DRY STACK GAS
VFT/AP4B

-------
CLIENT
PORT LOCATION
DATE _
                                                    VALINTINI FISHKR & TOMLINSON
                                                                ' WASMINOTOM
                                                            DATA SHEET
                                           IMPORTANT;   FILL IN ALL BLANKS
OPERATOR/S
RUN NO,
                                                                67-5

                                                           BAROMETRIC PRESSURE
                                                           AMBIENT CONDITIOHS^
                                                           PORT PRESSURE (Ps)_
                                                           PcM - PB * PS 	
                                                                                                                            f? /
                                                                                                                       "Kg
                                                                                                                      "H-d
SAMPLE ft METER BOX
METER BOX AH
FILTER nn.-/?-5-
                                                                                    ASSUMED MOISTURE.
                                                                                    C MTUM    —
                                                                                    REF. A P   —
                                                                                      -"Hg
                                                                                      ."Hg
CLEAN-UP NO/- '  ; BLANKS.
BOX & PROBE HEATER SETTING.
                                         SCHEMATIC OF TRAVERSE POINT LAYOUT
                                                                                                STACK DIMENSIOIS&JB; ARE*
                                                                                                PROBE NOZZLE OIA.J&-IN; AM '
                                                                                                PROBE LENGTH ___J__ FT
                                                                                                                /, /
                                                                                              .F2
                                                                                      JOiogSg. f2
                                                                                      	IN.
  INSTANTANEOUS READINGS:  RECORDED • BEGINNING OF TIME INTERVAL
                                                          AVERAGE VALUES READ WITHIN THE TIME INTERVAL
   CLOCK
   TIME
 (24 MRS)
ELAP.
TIME
(MIN)
                    DRV GAS METER

                     (CUBIC FEET)
DRY
TEMP.
INLET    OUTLET
BOX
TEMP.
CF)
IMPINGER
  TEMP.
  CF)
                                 POINT
PITOT VH
 ("H20)
ORIFICE  AH
   ("H20)
                                                    DESIRED
                                                      ACTUAL
 PUMP
 VACUUM
<-HgGA)
STACK
TEMP.
CF)
OPACITY
  OR
 XC02
                       7 7
  M.-*-?
                                                                                                                      /7o
                     ^Z,
                                                                               0/5'
                                                                                        •-ฃฃ-
                                                     A 5-9,
                                              7 a
                                                                                         01
                                                                                                                       ? 7
             /a
 M
             XT'
        G 7
                                              "? •*
             f
                                  .__Zฑ
                                               j*f
                                           . OJfl
                                            ro
                                                                                                                       To
                                                                                                                               c i -$"..
                                    312-
                                So/
                                                    //////
                                         f -
                                                                                                                         7

-------
                           VALENTINE,  FISHER & TOMLINSON
                     STACK  MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT

LOCATION

OPERATOR
                                                             RUN NO.
                                                             DATE
                                                                       NO.
 SAMPLE  BOX
H20 CONDENSED, ml  (1 ml = 1 gin)
     BUBBLER  (//I W/APPROX.  100  ml  WATER)

     IMPINGER (//2 W/APPROX.  100 tul WATER)

     BUBBLER  (ff3
U20 ABSORBED BY SILICA GEL, ml
 TOTAL  H20  COLLECTED,  ml
 VOL.  OF  H20 VAPOR  @  70ฐF.  AND  1  ATM.
 0.0474 x TOTAL
                                                   CONTAINER WEIGHTS
                                            FINAL
                                                             INITIAL
                                                                 .3
                                                               : 3
NET
                                                                      ~"  -
 MOISTURE  IN  STACK GAS,  %
 MOLE  FRACTION  OF  DRY  GAS
 MOLECULAR WT.  OF  STACK GAS
 % MOISTURE IN STACK GAS = 100 x VOL.  HpQ VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS =* lOG-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT.  OF STACK GAS = AVG. DRY MOL. WT. OF GAS X MOLE FRACTION 't-
                              is X (1-MOLE FRACTION)
VFT/AP3C
                                             100

-------
H
O
                       u
                                                                                                  3  —  ^ t l< /  iv /
CLIENTS
PORT LOCATION^
DATE  -^V/i/  .1^
                                  / CI -7
                                                           /•/-<
                                                                                                                         "Hg

                                                                                                                         . I
                                                                                            ..
                                      .mg
CLEAN-UP N0.<
BOX ft PROBE HEATER  SETTING.
                                  SCHEMATIC OF TRAVERSE POINT LAYOUT
                                                                 BAROMETRIC PRESSURE (PB)_JL2^-LJi	"Hg
                                                                 AMBIENT CONDITIONS i'ff>f/y	< /,',/./,-	
                                                                 PORT PRESSURE (Ps)	t2	"H20 -	
                                                                 PSN - PB + PS   -^'^	
                                                                 ASSUMED MOISTURE___ฃ_1_	
                                                                 C FACTOR  .63	,	
                                                           Z    STACK DIMENSIONS?^!/;
                                                                 PROBE NOZZLE DIA;7 V IN; AN
                                                                 PROBE LENGTH	FT	
                                                                                                                                                           .IN.
                                                                                                                                                                    . t\il
               INSTANTANEOUS READINGS:  RECORDED ป BEGINNING OF TIME INTERVAL
               CLOCK
               TIME
              (24  HRS)

                   X
              TOTAL,
               AVERAGE.
             ELAP.
             TIME
             (MIN)
             11
                           ij—.-

DRY GAS METER

 (CUBIC FEET)
                                           2
                                           -<*3-
                                   tป  * V.
                        31*. <-)?
                     f  ^ O  1  . \
                     c.-1) xit__i_^/__
                                             7
                                  .-:  ^
                                  ?.JfJ.- .'J V
 DRY
GAS
TEMP.
INLET
                                                   79
                                     ^1	
                                                     J7_
    OUTLET
                                                 79
                                                             >?
        -g.tr
        -B-fc.

BOX
TEMP.
CF)
                                                         3/0
                                                         "•'  -
                                                        XXX
IMPINGER
  TEMP.
  CF)
                                                                  C
                                                                              6 :>
                                                                  &> 0
                                                                             <:, z. .
                                                                 -A'.
                                                                            AVERAGE  VALUES READ WITHIN THE TIME INTERVAL
POINT
                                                                                      AT- 2-
                                                                                      o
                                                                                         -  '
                                                                                         -2.
                                                                                      n~
                                                                                         —-L
                                                    n  -  L
                                                    A.'JL
                                                    A-~1
                                                   "X/X
MTOT VH
 ("H
{&
                                                                                               /  s /  / /
                                                                                                .'-ป/
                                                                                                  .o/  S"
                                                                                        /
                                                                                       )/
                                                                                                - -P 7 S
          ORIFICE  AH
              ("H20)
                                                DESIRED
                                                                                                            / /  /  /
                                                       _i_a.
                                                                                                              -7 )' J

                                ACTUAL
                                                                                         V
                                                                                                                      ^_Cf^-_-
                                                                                                                          ~/~~
                                                                                                            o,
 PUMP
 VACUUM
("Hg GA)
                                                                                                                     -9, t-
                                                                                                                                 .•?,  o
                                                                            -Z^L
                                                                                                                                 .9..
                                                                                                                                 //,
                                                                             ,L-v_
                                                                              7^ O
STACK
TEMP.
                                                                                                                                          /  /  /
                                                                                                                                           -3 o ...
OPACITY
  OR
 XC02
                                                                                                                                                     / /  /  /
                                                                                                             . J /
                                                                                                            „:;/:>•
                                                                                                                             . J /
                                                                                                                               -J f
                                                                                                                               u,
                                                                                                                                                    '-•/
                                                                                                                                                    J /
                                                                                                                                                   0 /
                                                                                                                                                    ••V

-------
                          VALENTINE, FISHER &  TOMLINSON
                    STACK MOISTURE CONTENT  DATA AND CALCULATIONS
CLIENT
LOCATION

OPERATOR
-7
                                                             RUN NO.
                                DATE
                                                                      NO.   v '

                                                                      ~ - ->-'. /"?
SAMPLE BOX
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                INITIAL
H20 CONDENSED, ml (1 ml - 1 gm)
     BUBBLER (#1 W/APPROX.  100 ml  WATER)

     IHPINGER (#2 W/APPROX.  100 ml WATER)

     BUBBLER (#3 DRY)

H20 ABSORBED BY  SILICA GEL, ml


TOTAL H20 COLLECTED, ml


VOL. OF  H20 VAPOR ฎ  70ฐF. AND 1 ATM.  -
0.0474 * TOTAL  H2o


MOISTURE IN STACK GAS, %


MOLE FRACTION OF DRY GAS


MOLECULAR WT, OF STACK GAS
   MOISTURE IN STACK GAS - 100 x VOL.  H20 VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS - lQQ-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT.  OF STACK GAS - AVG. DRY MOL. WT. OF GAS yi MOLE FRACTION +
                              18 y. (1-MOLE FRACTION)
                                                                       NET
                                           A  7
                                           JO*  /
VFT/AP3C
                                        102

-------
                            ^, FISHER & TJMLINSON
                  ORSAT JATA AND CALCULATION SHEET
CLIENT ฃ-PA F/tfZ- T^^t-^'Z.
SAMPLING POINT
DATE •j'uly 3O . .
TIME OF SAMPLE
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100-Above)
LOCATION //T- S—+^.*r F^y~

'-/•-^^/

/.-ซx. HOW COLLECTED ฃ>*A 3 3*O /=:^/^-
COLLECTIO^
ANALYSIS
#1
.^
-20. ft
•2.&* 8




#1
/*/
10,4
O ป O




1 TIME OF ANALYSIS ^/u/\ 3/. /ซ^7i '
ANALYSIS
^
-20* 8
.20. 8




#2
/ S
l.o3
0,0



ANALYSIS
#3
ANALYSIS
#4
^ . ^'
^o.<3 ! 10. e
20. 8
0 \
                                                 WT. DRY STACK GAS
VFT/APAB
                                         103

-------
CLIENT
                     VALENTINE, FISHER &  TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
-c, r* t- +>
SAMPLING POINT LOCATION   /rf err ฃT#.  &

DATZ 7/3<->/75"^   RUN NO.

TIME OF SAMPLE COLLECTION
                    HOW COLLECTED  ev^/_j
TIME OF ANALYSIS
                                     7/3 ; /
7 IT
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + p2 + CO




COMPONENT
Z BY VOL. (DRY)
C02
02
CO



N? (100-Above)
ANALYSIS
#1
(2.0
*2-t.o
^/.<-




#1
O
^-LO
O, O



??.o
ANALYSIS
n
0. 0
Jt/.O
l/.o




n
o
ZiiO
0,0



?5,o
ANALYSIS
#3
*.&
3&- <8
lo.S-




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0
7o.g
0.0



79,?
ANALYSIS
M







#4









AVG.

20.53?
0,O



TSotf

RATIO \WT./MOLE
MOLE WT\ (DRY)
4A/100
52/100
28/100



28/100
AVG. MOLECULAR
0,O
L.tifi
OiD



a2,/3e?
ae.ซ^/
                                                   WT. DRY STACK GAS
VFT/AP4B
                     .04

-------
                         VALENTINE,  FISHER & TOMLINSON
                LABORATORY  ANALYSIS  AND TOTAL PARTICULATE  SHEET
CLIENT ^ p/Z   is fPjf ^/_ ^ Cฃ~	 DATE OF ANALYSIS    ~7~ 3Q-7

EVALUATION LOCATION >? '/ฃr*ฃS~-/f~  -^/^'•  ^-:./• Cฃ~      RUN  NO.   &	

EVALUATION DATE    *7 — 3>O — 75		     CLEAN-UP SET NO.    ^ *?- ,:T^
I.   EVAPORATION  OF      -?& _ (ml) OF
     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL 7:7^7 -2- /(mg) - TARE  77 ? ^ *% ฃ?       (mg)

          -BLANK ((.JOS 7  ing/ml) (  "7^    ml) =_L_^=__ mg )       =   "7. 7     mg.

 II.  FILTER CATCH _ # _ (Media  Type &  #)

                         /  (mg) - TARE     .3^jr. "T       (mg)       =  <*?.Q /     mg.
 III. HYDROCARBON OBTAINED BY ETHER-CHLOROFORM  EXTRACTION ON
     WATER IN IMPINGER AND BUBBLERS.
FINAL
-BLANK
IV . PARTICULATE
IN IMPINGER
FINAL
-BLANK
V . PARTICULATE
(mg) - TARE
( mg)
FROM EVAPORATION OF
AND BUBBLERS FOLLOWING EXTRACTION
(mg) - TARE
(( mg/ml) (
ml CONDENSED = ml)
FROM (ml) OF
BUBBLERS, AND CONNECTORS AFTER FILTER:
FINAL (ma) - TARE
-BLANK
VI. TOTAL PARTII
BLANKS
ACETONE =
(( mg/ml) ( ml) =
3ULATE = I + II + III + IV + V
mg/ ml =
ETHER-CHLOROFORM = mg. (FINAL
WATER- =
VFT/AP9 A
mg/ ml =

(mg)
" mg.
(ml) WATER
(mg)
ml initial
mg) = mg.
RINSE OF IMPINGER,
(mg)
mg) = . mg.
= // ?/ mg.
FINAL rag-
me /ml TARE mg.
mg - TARE mg)
mg/ml. FINAL mg.
TARE mg.

                                                                            JN
                                            105                            Z^-

-------
CLIENT
                        PL AC
PORT I OCATIQN
DATE Auf,
               U T S ID c7
                                         V
OPFRATOft/S.
RUN NO.  x
                      Z.
SAMPLE & METER BOX
METER BOX  AH  //
FILTER NO. ^"8-5~
CLEAN-UP NO.72-5^ -t
BOX & PROBE  HEATER SETTING
                 VALENTINE FISHER & TOMLINSON
                      SEATTLE. WASHINGTON
                    TRAVERSE SAMPLING DATA SHEET
                    IMPORTANT:  FILL IN  ALL BLANKS
                                                                                       t '
                                                                                  BARJ)METRIC PRESSURE
                                                                                  AMBIENT CONDITIONS
                                                                                                                                            "Hg
                                                                                  PORT PRESSURE (Ps) O    "HoO -_
                                                                                  PSN • Pfl * PS   y '•>' <>-' /	
                     TARE.
       3*c^ff  ^7-^"
                                   /jO
                                                                                  ASSUMED MOISTURE.
                                                                                  C FACTOR _/L^Z-
                                                                                  REF.AP_^_
                                                                                                                                            "Hg
                                                                                                                                            "Hg
                                                                                                                                             I
                                                        SCHEMATIC OF TRAtfFRSF POINT 1 AVOIR
                                                       STACK DIHENSIONSiii^i; AREA /./?•>   ft
                                                       PROBE NOZZLE DIA.^JjZlN; AH • -> >'  U  F*
                                                       PROBE IFNGTH    ?     FT.  ?	IN.
  INSTANTANEOUS  READINGS:  RECORDED 9 BEGINNING OF TIME INTERVAL
                                                                           AVERAGE VALUES READ WITHIN THE TIME  INTERVAL
   CLOCK
   TIME
 (24 HRS)
             ELAP.
             TIME
             (MIN)
 DRY GAS METEK

  (CUBIC  FEET)
 DRY GAS TEMP.
INLET
OUTLET
BOX
TEMP.
CF)
IMPINGER
  TEMP.
  CF)
                           POINT
PITOT VH

 (MH20)
  ORIFICE  AH
DESIRED
ACTUAL
 PUMP
 VACUUM
("Hg 6A)
STACK
TEMP.
CF)
OPACITY
  OR
 XC02
                                        C  - i
LJL
         ILL
                                                                                  s s  s s  s
                                                V
                                                                          A- 1
                                                                                              /  s /
                                                                                                        /  / 7
                                                                                                                    /  s /
                                                                                                                   A 2.

                                                                         A.
                                                                                                                  ^S	
                                                                                                                  -?A 
-------
                          VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT
             f\   P
LOCATION

OPERATOR
                                •$ 10
RUN NO
                                                            DATE
.   7
         NO.
SAMPLE BOX    .&ฃ/<
H20 CONDENSED, ml  (1 ml = 1 gm)
     BUBBLER (#1 W/APPROX. 100 ml WATER)

     IMPINGER (02 W/APPROX.  100 ml WATER)

     BUBBLER (03 DRY)


 H20 ABSORBED BY SILICA GEL, ml
                                                  CONTAINER  WEIGHTS  (gm)
                                           FINAL
TOTAL H20 COLLECTED, ml
 VOL.  OF H20 VAPOR
 0,0474 x TOTAk H20
                       *F^  AND l ATMf
 MOISTURE IH STACK GAS,  %
 MDLE FRACTION OF DRY GAS
 MOLECULAR WT.  OF STACK GAS
                                                             INITIAL
                                                                5-
                                                           b
          NET
                                                                           ..•t
                                                                           /
 % MOISTURE IN STACK GAS ป 1QO x VOL. H^Q VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS - 100-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT. OF STACK GAS ป AVG. DRY MOL. WT. OF GAS X MOLE FRACTION +
                              18 X (1-MOLE FRACTION)
 VFT/AP3C
                                            107

-------
                          VALENTINE, FISHER & TOMLINSON
                 LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ^T^S-   /=•/ ~zr -.-.'-   /-""	 DATE OF ANALYSIS  /? --  <$— 7_ET

EVALUATION LOCATION   A y•/.-^ ^ /> ฑ    /er- //:? ~~; ^/. /;.- ^—  RUN NO.      ~7	
EVALUATION DATE   eg? ~3 — ~7 Jb   '	 CLEAN-UP SET NO.   "7.? - 5"'
I.   EVAPORATION  OF    ^Q _ (ml) OF  /  ~/T ""ฃ // =T~

     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL 7ฃ'^ T -~ •'.• (mg) - TARE 7^a ••--ฃ. j _ (mg)

          -BLANK ((. G<~>5"7  mg/ml) (  ^ ^    ml)  - q ^~   mg )           ^> 5      mg

II.  FILTER CATCH   WSA   /JO-^B/; _ (Media Type)
          FINAL  5*-43> 7   (mg) - TARE   4v2, 7. ^ _ (mg)      =   S-^.3     mg
          />ป     y SB, 3    *>j -        /71?. ^—         j
     WATER IN IMPINGER AND BUBBLERS.

          FINAL  7? ฃ&*).<}  (mg) - TARE   "7Vr"-5 7,3       (mg)

          -BLANK (      A  ฃ _ mg)                           =    /Q . 5—  mg

IV.  PARTICULATE FROM EVAPORATION OF    2. / O _ (ml)  WATER
     IN IMPINGER AND  BUBBLERS FOLLOWING EXTRACTION -

          FINAL  77<>)o8,4- (mg) - TARE   7 7  g ? 7, Z _ (mg)

          -BLANK C(.<^2g^  mg/ml) (     2./ ^ _ ml initial

          -    7. 0     ml CONDENSED -  .2 ฃ /    ml)  = ^. ฃ   mg)   =   /<9. 4     mg.

V.   PARTICULATE FROM Pfl    (ml)  OF .4ฃET3f/ฑ'  RINSE OF IMPINGER,
     BUBBLERS, AND  CONNECTORS AFTER FILTER:
          FINAL 7g7<96.^ (mg) - TARE  7 <=> 7 ^ ฃ./       (mg)

          -BLANK ((.ry-^ 7 mg/ml) (   g   mg.
     ETHER-CHLOROFORM -    •   _ mg.( FINAL 7^2 ;fr. "^  mg -  TARE 7-2."*-  7   mg)

     WATER  =    . -^ _ mg/ /*-V  ml -  .  _ ^ •? --• .:.   mg/ml .  FINAL? 6^73 - <^   mg.
                                                                 TARE 7iy?7 •• . g   mg .
VFT/AP9 A


                                            10*

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
                                                                     72.-
SAMPLING POINT LOCATION

                     RUN NO.
TIME OF SAMPLE COLLECTION S2 ** - J3 —   TIME OF ANALYSIS Aa& ฃ".
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + P2 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N7 (100-Above)
ANALYSIS
#1
0.2.
ฃ0.6,
2o.(o




#1
Oi*L
^O.cj
v.o



~)^<4
ANALYSIS
#2
0-2
2.0.6
^0.6




n
o,*L
Z0> +
o.o



7?^
ANALYSIS
#3
tf.Z
/ฃc?.7
20,7




#3
0^
ZLo*^
O.o



79,3
ANALYSIS
#4







H









AVG.
'?
20.V15
0/0



"Tf.^e

RATIO W./MOLE
MOLE WT\ (DRY)
4A/100
32/100
28/100



' 28/100
AVG. MOLECULAR
•OSft
4,^31
O.o



22-2^2
ze.s*
                                                   WT.  DRY  STACK GAS
 VFT/AP4B
109

-------
I-1
o
PORT LOG AT I ON
DATE "
                                        V 7"/av Sy O V
VALENTINE FISHER & TOMLINSON
     SEATTLE. WASHINGTON
    TRAVERSE SAMPLING DATA SHEET
   IMPORTANT:  FILL IN ALL BLANKS
          RUN NO.
SAMPLE & METER BOX NUMBERS_ฃ^.
METER BOX  AH   /,&•*{2.	
FILTER NO/" ^q-b"  9 TARE
                                                                                                                          -~rs\
BAROMETRIC PRESSURE  (PB)
AMBIENT CONDITIONS ^ A- 'i '^
PORT PRESSURE (Ps)_l2	"H20 -	
PSN " PB + P$    ''  ^  ">  s~
ASSUMED MOISTURE ~l<> $	
C FACTOR _i
REF.AP.^,
                                                                                                                                                        J'Hg
                                                                                                                                                         "Hg
                                                                                                                                                         "Hg
                                                 mo
CLEAN-UP NO .
                              BLANKS
          BOX ft PROBE HEATER SETTING
                                                         SCHEMATIC OF TRAVERSE  POINT  LAYOUT
                                                STACK DIMENSIONS?^L^-{ AREA /-/ 7.'•
                                                PROBE NOZZLE DIA.^^LeiN; AN .  ป< ?,(,
                                                PROBE LENGTH.
                                                                                                                                                                   1 r
                                                                                                                                                    VFT/APIE

-------
                         VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT
LOCATION

OPERATOR
                                     X/
RUN NO.
DATE
                                                                       .75-5
         NO.
                                                                           70
SAMPLE BOX   A
H20 CONDENSED,  ml  (1 ml  =  1  gra)
     BUBBLER  (#1 W/APPROX. 100 ml WATER)

     IMPINGER (#.2 W/APPROX. 100 ml WATER)

     BUBBLER  (03 DRY)


H20 ABSORBED BY SILICA GEL,  ml
 TOTAL H20 COLLECTED, ml
 VOL.  OF H20 VAPOR @ 70ฐF. AND 1 ATM.
 0.0474 x TOTAL H20
 MOISTURE  IN  STACK GAS, %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT.  OF  STACK GAS
CONTAINER WEIGHTS (gra)
FINAL
+3C.7
4*!,. *
~? ^ 7 ฐ>
•^ >_/ ' • /
i/g.6
INITIAL
+17. /
44ฃ.%
-337. 7
&;o.&

NET
3.6.
o, a
0,2
-7,2
/^^
aj-?
/.*


 % MOISTURE IN STACK GAS = 100 x VOL. H2Q VAPOR
                           VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY  GAS =  100-% MOISTURE IN STACK GAS
                                    100
 MOLECULAR WT.  OF STACK GAS  = AVG. DRY MOL. WT. OF GAS X MOLE FRACTION +
                             18 X  (1-MOLE FRACTION)
 VFT/AP3C
                                            111

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE  SHEET
CLIENT  x^:^/?  F= / # ฃ• RJ- AC ET _ DATE OF ANALYSIS  (g-f -- ~7-S~

EVALUATION LOCATION  X? VSA^^^T  f=-/A ^ PL.fi ^ฃT _ RUN NO.     *% _
EVALUATION DATE    lg-  3  -7S~	 CLEAN-UP SET  NO.    ~?3 -


I.   EVAPORATION OF    9Q	(ml)  OF   X).
     RINSE & BRUSHING OF NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL "77 J264ป.7(mg)  -  TARE  9 7 .2- ฃ. O*ฐ)      (mg)

          -BLANK ((. 003 ~7 mg/ml)  (  =) Q      ml) ^-5__mg)       =   3~. $?    mg.

II.  FILTER CATCH  /^)SA  MO&  & M _ (Media Type)

          FINAL <3ฃ. ^   (mg)  -  TARE   "^-2 Z.  ^ _  (mg)       =   /c3. -^   mg.
III. HYDROCARBON OBTAINED  BY  ETHER-CHLOROFORM EXTRACTION ON        ~  - !- -
     WATER IN IMPINGER AND BUBBLERS .

          FINAL -?&ฐ) ) 2.,} (mg)  - TARE   7 6  ^ CPQ.7    (mg)

          -BLANK (     /.  g _ mg)                           =     9- ^    mg
IV.  PARTICULATE FROM EVAPORATION OF   -2
-------
                     VALENTINE, FISHER S, TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
SAMPLING POINT LOCATION

DATE AUb 4. /97J"~  RUN NO.
           y_
TIME OF SAMPLE COLLECTION /ซg — -

                                                   STAC A-
                                         HOW
                                         TIME OF ANALYSIS
                                                                 S,
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
ฐ2 .
CO



N? (100-Above)
ANALYSIS
//I
0,4
20.3
2o.$




//i
O'l
-20, 
-------
CLIENT .^T
PORT LOCATION
           ^.AMBIENT
                                            VALENTINE FISl- ER & TOMLINSON

                                                 SEATTLE, V/ASHINGTON

                                                TRAVERSE SAMPLING DATA SHEET

                                               IMPORTANT:   FILL  IN ALL BLANKS
                                                                                  'BAROMETRIC PRESSURE (PB):

                                                                                   LEAK RATF  tO—   CFM  (3_

OPFRATOR/S "W. J

RUN NO.   '•?
SAMPLE & METER BOX NUMBERS^ i

METER BOX  AH  /> H '/-2.
           ... ~  ._  -/Jt/-
FILTER NQ..."> ~;y
                                                                                 /
                                                                                                                      A 0
                                                                              - 2.

    • •> /
                          6iJ	
                                      ?/
                                                                            //  -
                                                                                     r^2^_

    -t
                           -. /,5 9
                                       77

                                                      3J-  ~

                                                                            ?^-__3
                                                                                              ^.. •?..
                                                                                                  .'j
                                                                                                                                                       •:> -
                                                                                                                      / o
                                                                                         ซ
                                                  V7
                                                                                      ^^J 7
 '? 1 7
                                                  t .r
 /.r 7 -J
               34-
                                            .-V. S~
                                                                          ^^/
                                   7/7P
                            .  7 ^
                                                 77/77
                                                                                                            . 7 :J
                                                                                               /wj,r
                                                                                           7*.
               V-/
         7/c, .^^~

                                                               Z> - ซ7


                                                               /i  - 2
                                                                                                      JL_
                                                                                                      - 7
                                                                                                 <, '-/
                                                                                                        9
                                                                                                         / 7 ^
 - TOTAL'
                                                                                              7-
  AVERAGE
                                    / 7.? ?
                                                          . 'j

                                                                                                            /  ;.MH20
                          75- 'F
                                                                                     Pm • Pfl *AH  •  "^ -J>  -7 /   "Hg
                                                                                                     -*-  / •* f (/ •'
    X    //;>!,.I- '-/"'   >/•>./•* I 
-------
                          VALENTINE, FISHER  & TOMLINSON
                    STACK MOISTURE CONTENT DATA  AND  CALCULATIONS
CLIENT

LOCATION

OPERATOR
RUN NO.
DATE
         NO/ * "* O
SAMPLE BOX    &
H20 CONDENSED, ml  (1 ml =  1  gm)
     BUBBLER (//I W/APPROX. 100 mi WATER)

     IMPINGER (#2 W/APPROX. 100 ml WATER)

     BUBBLER (#3 DRY)


 H00 ABSORBED BY  SILICA GEL,  ml
 TOTAL H20 COLLECTED, ml
 VOL. OF HnO VAPOR @ 70ฐF. AND 1 ATM.
 0.0474 x TOTAL H2o
 MOISTURE IN STACK GAS, %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT. OF STACK GAS
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
INITIAL
NET
           a   ;?
           —' •  -.
  % MOISTURE  IN STACK GAS =  100  x VOL.  H^Q  VAPOR
                            VOL. DRY GAS + VOL.  WET GAS
 MOLE  FRACTION OF  DRY  GAS  =  100-%  MOISTURE IN STACK GAS
                                      100
  MOLECULAR WT.  OF  STACK GAS  = AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION
                               18 X  (1-MOLE FRACTION)
                                              115

-------
                          VALENTINE, FISHER & TOMLINSON
                 LABORATORY ANALYSIS AND TOTAL PARTICULATE  SHEET
CLIENT   ฃ:p>A   F"Sฃ> ~-=>^ /"   ~	 DATE OF ANALYSIS  3 - ~7 - 7*.

EVALUATION LOCATION   ^  i/f^^ /-.^   !- /Pg^/. /^ C. T       RUN NO.     ~;
EVALUATION DATE       c$>-^-7_T'              CLEAN-UP SET  NO.     "7 <=ฃ• __^
I.   EVAPORATION OF   ^<2 O _ (ml) OF
     RINSE & BRUSHING OF  NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL ~7S 7.-? fZ.3 (mg)  -  TARE  7 P 770-  j? _ (mg)

          -BLANK ((j_ฃฃ5J7_mg /ml)  (  / o g    ml)  = . ^   mg)       = /?ป 9- _ mg

II.  FILTER CATCH   /V ฃ/y  //O.'g  ^2 /V     (Media Type)
          FINAL  ^73. C  (mg)  - TARE   3 5~CT. ฃ _ (mg)       =     / 3      mg
                                             ~> 7
                                                                    -     / r ?
III. HYDROCARBON OBTAINED  BY  ETHER-CHLOROFORM EXTRACTION ON          - —
     WATER IN IMPINGER AND  BUBBLERS.

          FINAL 79j-^7..~ (mg)  - TARE  7?5~5" 7. 5^    (mg)

          -BLANK  (      /. a _ mg)                           =    8. 2.     mg

IV.  PARTICULATE  FROM EVAPORATION OF     ^2 S~ /     (ml) WATER
     IN IMPINGER  AND BUBBLERS  FOLLOWING EXTRACTION -

          FINAL 77065.3 (mg)  - TARE  7 7(? S~ O .^     (mg)

          -BLANK (( .OQ2.S ^  mg/ml)  (     ^ ^ ./ _ ml initial

          -   /A 2.    ml  CONDENSED  = 23^.^  ml)  -  . 7   mg)   =    / 7.  Z    mg.
V.   PARTICULATE FROM  XO^^  (ml) OF  ฃC<ฃ73'/ ' ฃ"   RINSE OF IMPINGER,
     BUBBLERS, AND CONNECTORS AFTER FILTER:

          FINAL 7g/,; f.7  (mg)  - TARE 7i?C? j -    ml = 0. ฃ0>S* /   mg/ml    TARE    7gr^ f. ^  mg.
     ETHER-CHLOROFORM =    / • €> _ mg.(FINAL7 ^ 2g<3. 7 mg -  TARE  7 9  2 75- f   mg)
     WATER =    .  4 _ mg/   /40   ml =  •  0 Q Z56   mg/ml .  FINAL 1 c ^73. ^  mg .
                                                                TARE    1 1. 6, -7 -? ~Q mg .
                                                                                ~
VFT/AP9 A


                                               16

-------
                     VALENTINE, FISHER 5. TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
             A .
                                                              74 -
SAMPLING POINT LOCATION

DATE 4u&. t/nX* RUN NO
                                         HOW
                                    09
TIME OF SAMPLE COLLECTION 9J  - //      TIME OF ANALYSIS At/69.  ~?.
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
ANALYSIS
#1
0..
-------
CLIENT
PORT LOCATION^

DATE^
               /- /AV
                          XK ฃ.
         7Sn AMBIENT CONDITIONS /Iv/xf
        VALENTINE FISH ER & TOMLINSON
             SEATTLE. V/ASHINGTON

            TRAVERSE SAMPLING DATA SHEET
           IMPORTANT;  FILL IN ALL BLANKS
                                                                                        'SAROMfTfilC PRESSURE
                                                                                                                                A 7
OPERATOR/S
RUN NO.	
SAMPLE i METER BOX MiMRFRJV fiErl

METER BOX  AH  /-
FILTER NO.  3V-~T
CLEAN-UP NO.  ^-^

BOX & PROBE HEATER SETTING
                                                  iJ j ซv i
                                                      *
LEAK RATE - <> -2- CFM A
PORT PRF5-JIIRF (Pj) ^
PCM-PB + PS .-? V, '/^
^5""
"Hofl -
'J
"HG
"Hg
"Hg
                                                               ,n
                                                                 k.'
                                                        SCHEMATIC OF TW VERSE  POINT LAYOUT
                                                                                        ASSUMED KOISTURE_aL_2_X MAX VH.
                                                                                        C FACTOR X^r>

                                                                                        REF. A P--*

                                                                                        STACK DIMENSIONS^
                                                                                        PROBE NOZZLE

                                                                                        PROBE LENGTH
                                                                                                                                          "H,0
                                                                                                                            JAREA /• -' 7.-'  F2
                                                                                                                         JiilN; Kn^'J >- >V

                                                                                                                                    SIOE^Z,
  INSTANTANEOUS  READINGS:  RECORDED ป BEGINNING OF TIME  INTERVAL
                                                                          AVERAGE VALUES iREAD WITHIN THE TIME  INTERVAL
   CLOCK
   TIME
 (24 HRS)
             ELAP.
             TIME
            .(MIN)
        DRY GAS METER

         (CUBIC FEET)
                                        DRY GAS TEMP.
                                      INLET
OUTLET
          BOX
          TEMP.
IMPINGE!)
  TEMP.
  CO
POINT
PITOT VH

 ("H20)
ORIFICE  AH
    ("H20)
                     DESIRED
        ACTUAL
 PUMP
 VACUUM
("Hg GA)
                                                                                                                            STACK
                                                                                                                            TEMP.
OPACITY
  OR
 XC02
                                                                                                                                                 c; - 3
                      7/.V
                                     7-54
3
                     7/ -9.
   ^ 7
                            / 7
             / 2
                           . /
                        ^7. i- 3
                                                 /
                                                7 /
                                                                3'c)
                                                                         ^--  /
                                                                                    _0.
                                                                                 - sy'
                                                                                                                           -2/0
            -J /
                      7-2 ? ,
                      •7^/.  .).!
                                       J2L
                          !,  ^  7
                                                          5-(;
                                                                        <^_?
                                                                                  ^ ^/j?^,
                                                                                                                 /. -
                                                                                                                 irf"
                                                                                                                   , o

                                                                                               -y-
                                                                                                                             /^
                                                                                                75-
                                                           <::  - /
                                                           c- 2
                                                           <.'  - -3
                                                                                                        -  ,? -y
                                                                                                                  /, -5
                                                                                                                  •y }
           J^J
            -/,
                                                                         c ' -
                                                                                                        Ac^

                                                                                                              -3o >~
                                                        ^ d'.-

                                                                                               -C 6
                                                            ^
                                                                                               A /
                                                                                                         /.
                                                                                                                             /7s~
                                                                                                                 -V

                       ^d-
                       /^ /AJJ
                                                        .Jt:  T
                      "S-77.7
                                                        -275"

                                                          7.9

                                                                                  ป ~> 2 2
                                                                                    V +.0
                                                                                                        .. 94
                                                                                        O
                                                                                                   ^V
                                                                                                                   . V
 TOTAL'
  AVERAGE
                                       v;-/  k;-  •••
                                                                                          z:

                                                                                 Pin • PB +AH  "  79^7 ^  "Hg
                                                                                                                                               ..^//>~

-------
                          VALENTINE, FISHER  & TOIJLXNSON
                    STACK MOISTURE CONTENT DATA 400  CALCULATIONS
CLIENT  6 P /h
RUN NO.   /O
LOCATION _ฃXT5/t/5Vg>^/

OPERATOR
                                                                      NO.
                A/
INITIAL
                                                                       NET
               . 2.
  % MOISTURE  IN STACK GAS -  100  x  VOL.  H20  VAPOR
                            VOL.  DRY GAS + VOL,  WET GAS
  MOLE  FRACTION OF DRY GAS -  100-X  MOISTURE IN STACK GAS
                                      100
  MOLECULAR WT.  OF  STACK GAS  -  AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION +
                               18 X  (1-MOLE FRACTION)
 VFT/AP3C

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ฃT/ฐ/4   F/PฃZLfit.~	 DATE  OF  ANALYSIS  g - 7- ~7 ^

EVALUATION LOCATION   A >/ฃ-.-ป/> <<, ~  f= //ปg"J>'../•-•: .-"       RUN NO.   / &
EVALUATION DATE    8 - ^ - 7 JT~	 CLEAN-UP  SET  NO.    7JT-.S""'
I.   EVAPORATION OF   /O "7	(ml) OF
     RINSE & BRUSHING OF NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL  7'38'fr,..*.  (mg)  -  TARE  7 ^ & 3 2^ g      (mg)

          -BLANK (( . DOS'7 mg/ml)  (  / c 7   ml)  - . ฃ>    mg)       =  ~Z ฃ	 mg.

II.  FILTER CATCH  /V<^xJ  .//0g;  /g >/      (Media Type)

          FINAL 382. 6   (mg)  -  TARE    3^7. /	  (mg)       *   /ฃ". S~~   mg.
III. HYDROCARBON OBTAINED'BY-'ETHER-CHLOROFORM EXTRACTION Oil"      " 	*-'•  /	/>^.
     WATER IN IMPINGER AND  BUBBLERS.

          FINAL 7-7S33,J  (mg)  - TARE  77.T 2. 3 ^	 (mg)

          -BLANK (   / - 3	mg)                           =    / ^. ^    mg.

IV.  PARTICULATE FROM EVAPORATION OF      -^ป Q    (ml) WATER
     IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
          FINAL 78 bG b. *)  (mg)  - TARE   7 S^~ -3~3.6      (mg)

          -BLANK ((^CPQZg^ mg/ml)  (     ^6.^? _ ml initial

          ~   -"7" ^     ^ CONDENSED -  -S'S'P. ^ml) -  > 7   mg)    *   2 2 . -f-    mg
V.   PARTICULATE FROM  /^ 9  (ml) OF  4CE7Bsjฃ~ RINSE OF IMPINGER,
     BUBBLERS, AND CONNECTORS AFTER FILTER:
          FINAL 77 g ^7,^  (mg)  - TARE  7 7c?3 g .9        (mg)

          -BLANK (( . oo .T 7  mg/ml)  (    / 2 7  ml)  - . "7   mg)        ซ   ^ ^      mg

VI.  TOTAL PARTICULATE  -  I + II + III + IV + V                      -  // .5,  ,?   mg

     BLANKS
                                                                FINAL -7Q-1t.ฃ   mg.
     ACETONE -   dOg _ mg/_/ฃฃ__ml ป  a.ggS?  mg/ml    TARE   TST^T.^  mg.
     ETHER-CHLOROFORM =   /. ฃ _ mg. (FINAL 79Z&O mg -  TARE  "? i   mg .
                                                                TARE  769 73 .g~ mg .
VFT/AP9 A
                                           120

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT <ฃ"./ป A .
SAMPLING POINT LOCATION

DATE/[*iฃ  &./47S~ RUN NO.
TIME OF SAMPLE COLLECTION/i
                            '* -
                                         HOW
                                      —  TIME OF ANALYSIS
                                                                .  7
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
ANALYSIS
#1
0.+
20. ff
-2X
-------
                                          r   7ซ* * *>/ >
CLIENT

PORT lOCATl QNvg~X7-ฃA/jr
           5 AMBIENT CONDITIONS..
OP E RATOR/ '^zL^dA^Z.
RUN NO.  "ฃ&  //

SAMPLE & METER BOX NUMBERS ^ c (..

METER BOX  AH / rt-4-S 	

FILTER NO.  fx> ~~  9 'TARE
CLEAN-UP NO.
                    BLANKS.
    & PROBE  HEATER  SETTING
                                                        VALENTINE FISt- ER & TOMLINSON
                                                             SEATTLE, V/ASHINGTON

                                                           TRAVERSE SAMPLING DATA SHEET
                                                           IMPORTANT:  FILL IN ALL BLANKS
                                                                         -ft*
                                                         SCHEMATIC OF TR/VERSE POINT LAYOUT
       'BAROMETRIC PRESSURE (P0).

        LEAK RATE •ป.'?' t>" CFM 0_

        PORT

        PSN"
                                                                                                             PB
                                                                                                                                 MAX VH
        ASSUMED KfllSTURE --'y

        C  FACTOR/•_/	

        REF.AP ซ -"> 5   ,	

        STACK DlMFNS10Nsffฃ*/9J'AREA />

        PROBE NOZZLE DIA.i^ V IN; AN	

        PROOE IFMKTH-'^    Nll.-iBFR   /   SIDE
               _"HG
               _"Hg
               ."Hg

               MH,0
  INSTANTANEOUS READINGS:  RECORDED ป BEGINNING OF TIME  INTERVAL
                                                                            AVERAGE  VALUESiREAO WITHIN THE  TIME  INTERVAL
                                                                           POINT
PITOT VH

 ("M)
                                                                                                  ORIFICE  A H
                                                                                                     ("H 0)
                                                                                                DESIRED
                                                                                                          ACTUAL
                    PUMP
                    VACUUM
                    ("Hg GA)
 STACK
 TEMP .
OPACITY
  CR
 XC02
                                                                                                                                                 /*/.
                        f. c-3
                                                                          A - I
                                                                          A-*
                                                                          A_=_ฑ
                                                                                       */2.
jt-^_ii_
2^ฐฑL
^OSL
                                                                                                ..97
                                                                                                          L/o
                                                                                                                   -3~
                                                                                                         .  $0
                                                                                                                    "7.
                                                                                                +$3—
                                                                                                .37
                                                                                                          -97
                                                                             -2
                                                                                    ~ 6V
                                                                                                                    ~7.2
                              /_2i-_
                              -2^.42.
                                                                                                                              .105
                                                                                                                    7, s-
                                                                                                                     7, :>
                                                                                                                              /9c9
                                                                                    •. V / ^
                                                                                                          . 7/
                                                                                                                              /7s
                                                                            -/• /--
                                                                                     / —
                                                                                                       r
                                                                                                 .7') "H20 -0(5 "H
                                                                                                                                                  -;>' 0
                                                                                   Pm - PB
                                                                                                    2  V7&"  "H9

-------
                          VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND CALCULATIONS
CLiฃNT
                                                            RUN NO.  //
LOCATION

OPERATOR
                        f o 
-------
                         VALENTINE,  FISHER & TOMLINSON
                LABORATORY ANALYSIS  AND  TOTAL PARTICULATE SHEET


CLIENT   /ฃ•/=>/!  /=/*?FP? ,f .^ (mg) -  TARE    7 g>  7 / 3* /   (mg)

          -BLANK ((eg. gg :T 7 mg/ml)  (_/_&J0_ ml)  = O. k  mg)      =  5".  J      mg.

II.  FILTER CATCH  /^_g x9  / /V3 ^,  & 4  % _ (Media Type & tf)

          FINAL 375". 3   (mg) -  TARE   37 O.  .5" _ (mg)      =  ^  ^      mg.

III. HYDROCARBON OBTAINED  BY ETHER-CHLOROFORM  EXTRACTION ON
     WATER IN IMPINGER AND BUBBLERS.

          FINAL _  (mg) -  TARE _ (mg)

          -BLANK ( _ mg)                           =        ~     mg .

IV.  PARTICULATE FROM EVAPORATION OF _ (ml)  WATER
     IN IMPINGER AND BUBBLERS  FOLLOWING EXTRACTION -

          FINAL _  (mg) -  TARE _ (mg)

          -BLANK (( _ mg/ml)  ( _ ml initial

          - _ ml CONDENSED =  _ ml) = _ mg)   = _            mg.

V.   PARTICULATE FROM _ (ml) OF _ RINSE OF IMPINGER,
     BUBBLERS, AND  CONNECTORS  AFTER  FILTER:
FINAL
-BLANK ((
VI. TOTAL PARTICULATE =
BLANKS
ACETONE = • 8
ETHER-CHLOROFORM =
WATER =

(mg) - TARE
ing/ml) ( ml) =
I + II + III + IV + V
mg/ / 4- Q ml = lOO S~~?
mg.( FINAL
mg/ ml =
V
(mg)
mg)
mg/ml
mg -
mg/ml .

_____
= SO. /
FI1JAL Jg-^lC'li.
TARE ~7 ฃJ •-- -*, :~". ;
TARE
FINAL
TARE
mg
mg
X
%R.
mg
nip;
VFT/AP9 A

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION  SHEET
CLIENT
SAMPLING POINT LOCATION

                     RUN NO.
                                         HOW  COLLECTED,
TIME OF SAMPLE COLLECTIONX^**7-  /to'-ฃ   TIME  OF ANALYSIS   ALfdป.  7
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO



ANALYSIS
#1
0.6
20. 6*
*j<*.8



ANALYSIS
#2
0.&
2^0. ฃ.
Z0.9



ANALYSIS
#3
O.^T'
2.O. 6ป
2.0. 7



ANALYSIS
#4






COMPONENT
% BY VOL. (DRY)
C02
#1 i #2
<9. (a 0. S
ฐ2 : 2CL<0
co \ 0. 2.

\

N? (100-Above)
78.2
30. /
0. Z



7S.Z
#3
^?, 5~
10. /
0. 1



#4






~7ง.3 \
AVG.
0. ^
20. /
O. 7



78*2.
RATIO \WT./MOLE
MOLE WT\ (DRY)
44/100
32/100
2a/ioo



28/100
AVG. MOLECULAR
.zz.
6,^32
,os~^



2/.8*ฑ
~? G ' n
— <3,0V
                                                   WT.  DRY STACK GAS
 VFT/AP45
                                         125

-------
CLIENT *VW 7-7-dV. /*>4f-ฃ.

PORT IOCATION & ^T^T/l/SV^ *./
DATE <^-/;
OPERATOR/S
RUN NO /-
?", AMBIFNT CONDITION^,
X?^-^^/^ /2-Tb /5*J/}AJ<0*/
?

VALENTINE FtSh ER & TOMLINSON
SEATTLE, V/ASHINGTON
TRAVERSE SAMPLING DATA SHEET
IMPORTANT: FILL IN ALL BLANKS
J.'7/ZrT- ^^ Cc>*4.
SAMP( F t MFTFR fifl* NIJMRFRS ^^7^ ^^ / ^ .-,.
MFTFR ROX AH / ' ^*
FILTER NO.-'
1^.
. _-- J?A-i ''<•'-> - -,
< ' - ^> ป TARE 5:5<ฃ • 7 nw
CLEAN-HP NO. 'V ; RIANKS ป


BOX 4 PROBE HEATER SFTTING -2*k''l .'>Cป1
2-* ^ /ฃ?.' 2.0
S7Z>P Q ^ ^^>T <*"x^ :sr0
SCHEMATIC OF TR/VERSE POINT LAYOUT
INSTANTANEOUS READINGS: RECORDED 9 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
9 ' 1^



/**\
Y; V-]


x ^^/
/^. /"
-y^f frt
-r&* •&
7f^> jr
TV 7 ^ s"
/^7-<*'9
7^>. 

-. /^ 7v y ^ >' P. vr fr^iU'xO F^'if. ,^' 60 s ",r P^<< x'f c^O/. c/ ^^V.^6^ . . . ^^,007 VX///X DRY GAS TEMP. INLET f > ^V ฃฃ_ _2.? •ป/?/ "3t *? ฃ'/<;$- C- 7 /F '70 •7//-7X. /? ?D~ 74/^r •7 7/T) 79 f^C"> /72v 7ft 'F - ^,?8*R BOX TEMP. CF) 2. s-C 2i"^" J246_ 2.<^2 2^ j2' 27^ " t-jc it 7 ^2f>- d s-c '/// /// IMPINGEIl TEMP. CF) 4o *^ ฐ •^o Vs" ^-- _^o_. "^ -li" •>"! ฃ-0 ' 5~-2 *i?> /// V/, 'B L P P A C R S P P AROMETftIC PRESSURE (P EAK RATE • <ฐ / CFM ORT PRESSU SN ' RB + SSUMED KOI FACTOR / ) 39 IV S "Hg a <> ^~ "HG RE (Pc) <~ "HoO - C"> "Ha P? '-; -' ^ >ฃ "Ha STURE /^ t MAX Vl| "HnO ^/ EF.AP .ฃ>-iC TACK DIMENSIONS'^/-/^'/ AREA V /. - F2 ROBE NOZZLE DIA.-Ji ROBE I FNGTH 3 ' NU IN: AH • ป . f2 '•iCFR /_ SIDE 4 AVERAGE VALUES:READ WITHIN THE TIME INTERVAL POINT At 2. 3 '} .&JL- 3. f3 -4 C / 3. 3 •V >' i ^-> ~^~ y// '/ PITOT VH CH20) o/ t-i+ <0/2. .0/, tv-f ^•, &<< ฃ>. C>i 3 &.C/ 2 &.0/1 O.Oi'* ;;___,. x/7// '////, ORIFICE AH ("H 0) DESIRED <^~ O. ฃ, 0> / o. s' p. z*~ e.fi o, B c\ < <-> < ฃ>. / o. 74 V-^ 0-* 4>. 7-f XT. f '• i>' ^•7 ^ซ / t;. /i -S' c* •*'*>' O' B f\ & — 7 — / AV,#j*H2o •7V "H20 -.oiT-Hg Pm " Pfl +AH - Jf) -i XiT "Hg PUMP VACUUM ("Hg GA) 'ฃ ,>u ฑ,0 7.e -2.S" ^^o 2^0 'l.D ? c' ^ U?^ 3.o 3-0 2,z ^/i" ?./ ^ * •7-^ ซi •3-^ ^. o ' - r- r — //>' - '//.-' STACK TEMP. CF) / 75 77^ /<5 i" f f~i~ / 7S' /A-JO /^o /?? / ?c nz 217C> rtc /M /&'~i /ฃฑ '?<." /p •;• /FA: / 77 ?S~;^ I7& 6 _?4 'ซ OPACITY OR SCO? — * 1 0 t C// sc'/3_ .ฃ>// 01 VFT/APl


-------
                          VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT
             P &
                                                             RUN NO.    /
LOCATION

OPERATOR
                                                             DATE
                                                                      NQ.7 •  "" O

                                                                      ~ B -
SAMPLE BOX
                                                   CONTAINER WEIGHTS (<&&)
                                           FINAL
                                                A
                                                  .  o
                                                             INITIAL
H20 CONDENSED, ml  (1 ml =  1  gm)
     BUBBLER (#1 W/APPROX. 100 mi WATER)

     IMPINGER (#2 W/APPROX. 100 ml WATER)

     BUBBLER (#3 DRY)


 H20 ABSORBED BY SILICA GEL,  ml


 TOTAL H20 COLLECTED, ml
 VOL. OF  H20 VAPOR @  70ฐF.  AND 1  ATM.
 O.OA74 x TOTAL  H2o
 MOISTURE IN STACK GAS,  %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT.  OF STACK GAS
 % MOISTURE IN STACK GAS • 100 x VOL. H30 VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS ป 100-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT. OF STACK GAS = AVG. DRY MOL. WT. OF GAS X MOLE  FRACTION
                              18 X (1-MOLE FRACTION)
                                                                       NET
                                                                       -2. O
                                                                       3.
                                                                       O,
                                                                       jr. 3
                                                                       //. 3
VFT/A3P3C
                                          127

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT ฃ1ฃ>A  /=/>?-• J^/tf r.ฃ"	 DATE OF ANALYSIS  #- r- 7

EVALUATION LOCATION   AXฃ>ฐ^ S* ^r  /= /. ^'T&t.S-Z^       RUN NO.  /
EVALUATION DATE    3~8~ 75~" _ CLEAN-UP  SET  NO.    "77—
I.   EVAPORATION OF    ^3 _ (ml) OF
     RINSE & BRUSHING OF  NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL 7 -)<} ^3 . 6(mg)  - TARE   ~7 7 O 3 8. & _ (mg)

          -BLANK (( , co S" ~7 mg/ml) (  ? c     ml) -  . 6    mg)           ^. Z.     mg

II.  FILTER CATCH   /K?^x?  //g?ฃ  /? //     (Media Type)
          FINAL ^c?^. 7   (mg)  - TARE   3^"^>"7 _  (mg)       =    4- 8      mg.
                /8J. *f   ^r,*)          '-7*9.3          (*ป&       *    3  J      m
III. HYDROCARBON OBTAINED  BY  ETHER-CHLOROFORM EXTRACTION  ON          - '-^~^ -
     WATER IN IMPINGER  AND BUBBLERS,

          FINAL 7 ^ *9 < "7./  (mg)  - TARE  7 "7 ^ ^ <5—      (mg)

          -BLANK ( _ /,  g _ mg)                            =    g?. g     mg .

IV.  PARTICULATE FROM EVAPORATION OF   X/^-~~ _ (ml) WATER
     IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -

          FINAL 7 7-2.5^.7  (mg)  - TARE  "77-2^ ซ3.ฃ       (mg)

          -BLANK ((.002.86   mg/ml)  (     2 ' J> — _ ml initial

          ~   //. J      ml CONDENSED - 3> 7  ml) -  . ฃ>   mg)    -  / C* • ฑ~    mg.
V.   PARTICULATE FROM/ 3^   (ml) OF /? g^~7Tr A/^T    RINSE OF IMPINGER,
     BUBBLERS, AND CONNECTORS AFTER  FILTER:

          FINAL? 7(3 ffc.2.  (mg)  -  TARE   7 7^~73.3        (mg)

          -BLANK (( . 00 5" 7 mg/ml)  (  / 3 C>    ml) - . 7    mg)        -    '^2.      mg.

VI.  TOTAL PARTICULATE -  I + II + III  + IV + V                      =•   7 g     mg.
     BLANKS
                                                                FINAL 7g:T56.6   mg.
     ACETONE =•   .  _ mg/  /  O  ml -  Q.O^T'?  mg/ml    TARE  ") 5r3sT 9   mg.

     ETHER-CHLOROFORM ป _ mg. (FINAL _ mg -  TARE  _ mg)

     WATER = _ mg/ _ ml - _ mg/ml.  FINAL _ mg.
                                                                TARE  _ rag.
VFT/AP9 A

                                        128

-------
                    VALENTINE,  FISHER & TOMLINSON
                  ORSAT DATA AND CALCULATION SHEET
CLIENT _

SAMPLING POINT LOCATION 	

DATE  tf/^/sS'   RUN  NO.  /' &-
                                              T^ฃr
TIME OF SAMPLE COLLECTION
                                        HOW COLLECTED
                                                                     /ss
                                        TIME OF ANALYSIS
                                                         #//

CUMULATIVE .
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
Z BY VOL. (DRY)
C02
02
CO



Nj (100-Above)
ANALYSIS
#1
6-3
-zo^
?&,
-------
CLIENT
PORT LOCATION^
DATE &/S1/ 7^AMBIENT CONDITIONS,
OPERATOR/S.
RUN NO	
                                        0*/
                                                         VALENTINE FISK ER & TOMLINSON
                                                              SEATTLE, V/ASHINGTON
                                                             TRAVERSE SAMPLING DATA SHEET
                                                            IMPORTANT:   FILL  IN ALL BLANKS
SAMPLE &  METLR  BOX NUMBERS
METER BOX AH_ฃ
FILTER NO.
                                   3
                                                              A
  TARE.
BLANKS .
                          B
                                                                                           'BAROMETRIC PRESSURE (PR).
                                                                                            LEAK RATF    O2   CFM Q_
                                                                                            PORT PRESSURE
                                                                                            PSN " PB * PS —'-
                                                                                            ASSUMED MOISTURE.
                                                                                            C FACTOR.
                                                                                            REF.AP_
                                                                                                                                      -  -> y S
                                                                                                                                   MAX VH.
                                                                                                                            "HG
                                                                                                                            "Hg
                                                                                                                          -MHg
                                                                                                                          _"K,0
                                                                                   12 :
CLEAN-UP NO. 7">
BOX 4 PROBE HEATER SETTING
                                                          SCHEMATIC OF TR> VERSE POINT LAYOUT
STACK DIMENSIONS^.
PROBE NOZZLE DIA.
PROBE LENGTH	'3_
.AREA.
                                                                                                                                          ' /  '
                                                                                                                  IN; AN
                                                                                                               .NUMBFR
                                                                                                                                         SIDF  /
                                                                                                                                                      C   i
                                                                                                                                                      o/
                                                                                                                                           VFT/AP1ฃ

-------
                          VALENTINE, FISHER  & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND  CALCULATIONS
CLIENT
RUN NOi    /3
LOCATION /^x

OPERATOR
         NO
                                                                        . •  Q " o
                                                             DATE
SAMPLE BOX
H20 CONDENSED, ml  (1 ml = 1 gin)
     BUBBLER (#1 W/APPROX. 100 ml WATER)

     IMPINGER (02 W/APPROX.  100 ml WATER)

     BUBBLER (#3 DRY)

 H20  ABSORBED  BY SILICA GEL, ml


 TOTAL H20 COLLECTED, ml


 VOL. OP H20 VAPOR @ 70ฐF. AND 1 ATM. -
 0.0474 * TOTAL H2o


 MOISTURE IN STACK GAS, %


 MOLE FRACTION OF DRY GAS


 MOLECULAR WT. OF STACK GAS
   MOISTURE IN STACK GAS ป 100 x VOL. H^Q VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS - lQQ-% MOISTURE  IN  STACK GAS
                                     100
 MOLECULAR WT. OF STACK GAS - AVG. DRY MOL.  WT. OF  GAS  X MOLE  FRACTION +
                              18 X  (1-MOLE FRACTION)
CONTAINER WEIGHTS (gm)
FINAL
^JtT-/
^i7 .e
3 2. 7, o
ฃcr-7. /
INITIAL
-V 57 
-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ฃ~..^>. x- .   /-TV /^Jf>-...  /?.: /-—DATE  OF ANALYSIS  ?'- g -
EVALI
EVAL1
I.
JATION LOCATION ^ / ~_; 	 	 /=• / & -~ ff / ^ •' -

RUN NO. / 3
JATION DATE ฃ - o _ -^jp CLEAN-UP SET NO. ~7r?- <—
EVAPORATION OF / / "7 (ml) OF AcETZ,

RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
FILTER.
FINAL ,5ปc?/-^^.7 (mg) - TARE # 3/J & • ^ (mg)
II.
QA
III.
IV.
V.
VI.
-BLANK ((.cjฃ>jr 7 mg/ml) ( // 7 ml) =
FILTER CATCH /V-S/4 //ob Z3 .V $ (Media
FINAL 37 , 3 -
WATER IN IMPINGER AND BUBBLERS.
FINAL7<^573.^ (mg) - TARE ~7b S~ 7/.O
-BLANK ( ^ <^ mg)
PARTICULATE FROM EVAPORATION OF <2/^>
IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION
FINAL 77g^S".2 (mg) - TARE 7 7 g 2 ^
-BLANK ((.J<^2tfa mg/ml) ( 2./-S —
_ ?. 5" mi CONDENSED - ^^5t^*ml)
PARTICULATE FROM / 2 O (ml) OF ^Cฃ~Tcy^ฃ'
BUBBLERS, AND CONNECTORS AFTER FILTER:
FINAL 7?3*)2?) (mg) - TARE "P7J 8 ซ . *7
-BLANK (( .ฃ>o 5" 7 mg/ml) ( / 2.O ml) -
TOTAL PARTICULATE = I + II + III + IV + V
BLANKS /f2/X-/ /^ X

ACETONE = mg/ ml =
ETHER-CHLOROFORM = mg. (FINAL
WATER = mg/ ml =

(mg)
= ^ . ^e> mg .
(ml) WATER
? (mg)
ml initial
= • Co mg) = / S~ mg.
RINSE OF IMPi:iGER,
1 (mg)
• 7 mg ) = ,S"~. ? ing .
"T & mg .
FI:;AL mg .
mg/ml TARE mg.
mg - TARE mg)
mg/ml. FINAL mg .
TARE me .
VFT/AP9 A
                                              132

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
SAMPLING POINT LOCATION
DATE   &
                     RUN NO .  / 3-
                                         HOW COLLECTED
TIME OF SAMPLE COLLECTION
                                         TIME OF ANALYSIS  37 // r?~
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + co




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100-Above)
ANALYSIS
#1
0,3
10, tf
2o, 
-------
VALENTINE FISHER & TOMLINSON
CLIENT ฃ" &A f, g-r f>{W S~
PORT LOCATION rf*-"?r<-/"'<-<- ft A><~^' TV'VQ- ^
DATE K/' ' 7
•""AMBIENT CONDITION*:. "V. '•'i/.' 7 ;' S//W7,-/x>
RUN NO. /'/
SAMPLE i ME1
METER BOX -fi
FILTFR NO.-
FER BOX HUM
H / v-
BERS ,1 & Qt-'K-f^

?6-lT 0 TARF .'>V-S~ '/ ma 5~-~
CLEAN-UP NO. 7 '/-*>'; Bl
BOX J PROBE HEATER SET
ANKS •- & '
FTING 2 iV 4
SEATTLE, V/ASHINGTON
r^/^>->r



/ -,.'./-/



•'/ '.








/TOTAL*/7/
x AVERAGE-'
ELAP.
TIME
(MIN)
c^>
'$
X
Cj
1?
/•v
/ฃ4
-2/
•M
,? 7
'><-•
.•> ~>
' V
.>••;


-/ •?
A /
V/
•^ /
, f




c- /->
'////
DRY GAS METER
(CUBIC FEET)
"
r "ff-1' ("' *} -~i

f V /. 'T'V'
fr\7 o , /
^f •? c>
^c|^ ^
t^6.x:i *>'
f-t 7 . 7
Fr/ .2
t:'^.\'-' -^
t^'//. ^
•r' ' ; \ q
r''H . l| '".
b'V'o . -.'
^"•- ?. *-;
>.*• > i- . l|V
ซ^'c r ^
(^•/ /. 7
Z~ ' i* ' ฃ V C*'
.'-• .'-/.-?
^_ *. *"> i j i




,//. ..^.^
'//////
DRY GAS TEMP.
INLET
7<^>
7/
-7 /
1 '•>
v /'A
TS
fei /
P ^'
^'7//
5r'-/r
<7/
*T ^
C/'J ฐ '
V 1
*"/ฃ"•
-v. . y.
vV -- ' '•
V •,"•
7^j V-.
^ •/
/ c^ ' '




-'/^•;
OUTLET
<ฃ>:'
•^•^
/•/!
'73
'?•>
7C,
V 7 "* "
o'"
f-'c>
ฃ•>' /
t'-/ /.-• i
^>r
j"1' *-~
$• :
t~ (.-




/A X,


Z'O
il-j O
-^f
^70
l>^Jo
2 ->' . ~
.^^C)
i?-Vซl
'.S" c-
:> /<
:'-V^>-
.^ /•>
.,' S'-s, •
,.ปc -r
i!v*" C1
^-;^





/ /~ / /
f / /
IMPINGED
TEMP.
(•F)
•A?
41::
^
c6.
to
<^t:
,^- :

-^ 7
< /
"•=S:
.




'///
y//;
. .,-• * ~
j'f

'BAROMETRIC PRESSURE (P
LEAK RATF -C 1 rFM
P
P
A
C
R
n) ' ' "H9
U' T
a "' ^ "Mf.

DRT PRF5SIIRF ^Pc^ ซ•'' "HoO - f- "Ha
SN " PB +
SSUMED MOI
FACTOR /,
5S ' / . "Ha
STURE / ' - "i MAX VI
/
1 	 JUป0
EF.AP. Cl'l

STACK DIMENSION^ :''V^ AREA ' F2

/- '
:RSE POINT LAYOUT
PROBE NOZZL
PROBE LEN3T
F niA, '/.? IN; AN . F2
H '">' ' NUMBER .._./. SIDE -^ .„
AVERAGE VALUES '.READ WITHIN THE TIME INTERVAL
POINT
A \
^
"^
'-7ฑ-_
•->
-I
c /

••i
"1
'r.1
.•>
•7
7
•^ •
^
—dL-


'~r-7~.
'(>
'///

PITOT VH
("H20)
^ / / / /

. c - -^r
./••ซ'•<ฃ'.
iV.'.t''.
f^/
. r/.:'
c V '-?
f /o
^d'1 ฃป'
. r.vH
C'/f
. o/->
- .-.' /
,(."//
C'l "3
.<:•>//
'"• /
•f/ /

f /




x / ./ /
////,
/////
ORIFICE A H
("H 0)
DESIRED
/ / / /
:}#
• 2 r'
,-^c"
v>|
. - -
^ • /
7 s, -
.S :>
• -7 s ~

?•'
.#•-."
. -' /
C- '-'
• 7 .!

. ^.c
( '•"
f. •>
. -^



•7-r-r-
////
ACTUAL
./ / f /
. ' *•
2 t't
•&' .
- M

(- cry
. /r
. V 'i
• --1 <•; ~
c ป
f>
.$•••-••
V.' ,'
c ^
•f-t
^ c
. ••" c
^ '>
c .•>
. - <



r-7—r-,
/7,'/TH2o
0,/^-"H20 Vr -/"Hg
Pm • PB *^H • , ' > "Hg
PUMP
VACUUM
("Hg GA)
/ / s /
1 <.>
1 . c.'
/. v
/ •'.'
2 . o
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0 J
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// /

STACK
TEMP.
(*F)
"^ **ซ/•ป>
/(•• '•>
/ /c-
7-.) y
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/ 1- - '
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/ ^~
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OPACITY
OR
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f f. r


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c




                                                                         _.   .t /
                                                                              c  /

-------
                          VALENTINE, FISHER &  TOMLINSON
                    STACK MOISTURE CONTENT  DATA AND CALCULATIONS
CLIENT
                                             RUN NO.  .^
                                                                      79-5
LOCATION _^f'/-r ?.*._-~ *   X?>f~--'.

OPERATOR
                                             CLEAN-UP NO.

                                             DATE  ^ ~ / 2
SAMPLE BOX
"r-f
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                             INITIAL
H20 CONDENSED, ml  (1 ml = 1 gm)
     BUBBLER (#1 W/APPROX. 100 ml WATER)

     IMPINGER (#2 W/APPROX.  100 ml WATER)

     BUBBLER (#3 DRY)


H20 ABSORBED  BY SILICA GEL, ml


TOTAL  lUO  COLLECTED, ml


VOL. OF  H20 VAPOR @ 70ฐF. AND 1 ATM. -
0.0474 x TOTAL H2o


MOISTURE IN STACK GAS, %


MOLE FRACTION OF DRY GAS


MOLECULAR WT. OF STACK GAS
 % MOISTURE IN STACK GAS = 100 x VOL. H2Q VAPOR
                            VOL. DRY GAS + VOL. WET  GAS
 MOLE FRACTION OF DRY GAS = 100-% MOISTURE  IN  STACK GAS
                                      100
 MOLECULAR WT. OF  STACK GAS  = AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION +
                              18  X  (1-MOLE FRACTION)
NET
 VFT/AP3C
                                             135

-------
                         VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE  SHEET
CLIENT
EVALUATION LOCATION  X?

EVALUATION DATE
                                                DATE OF ANALYSIS   f — //Z-"7S"

                                    /~. r* --!_/- :  ~       RUN NO.
                   3 - / ,3. — 75"
CLEAN-UP SET NO.   / 7—
I.    EVAPORATION OF
                                 (ml) OF
     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL 7 7/03.7  (mg) - TARE

          -BLANK (( . &QS-7 mg/ml) (  /

II.   FILTER CATCH   /M cf?<ฃ>
-BLANK ( /; ,9 mg)
IV. PARTICULATE FROM EVAPORATION OF ^ ^ 3
IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION
FINAL^fi^B.-? (mg) - TARE 7 576s 3. C
-BLANK ((.0^25 a mg/ml) ( 2 5~ 3
/ •*ฃ• 7 ml CONDENSED = 238.3 ml)
V. PARTICULATE FROM /; 7 (ml) OF ^<^ฃ 7cJ//ฃ"
BUBBLERS, AND CONNECTORS AFTER FILTER:
FINAL7773<ฃ
-------
                     VALENTINE,  FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT ..ซr .
SAMPLING POINT LOCATION

DATE   8// 1 /~> ^~~ RUN NO.

TIME OF SAMPLE COLLECTION
                          #o'<'*
                                         HOW COLLECTED St.* -*•'.•
                                         TIME OF ANALYSIS
CUMULATIVE  .
% BY VOL.(DRY)
C02
C02 + 02
C02
         + CO
               ANALYSIS
                  #1
                          ANALYSIS
                             #2
                          2*.
        ANALYSIS
           #3
                                                ANALYSIS
                                                   #4
       Z/,0
COMPONENT
% BY VOL. (DRY)
                  #1
#2
                                       #3
                                                  #4
AVG.
RATIO  wT./MOLE
MOLE WT\ (DRY)
C02
                            a.
                                      o,
                                    44/100
02
                                      20.5-
                                    32/100
CO
                   o
                                                                 23/100
    (100-Above)
                "79- 2.
         ~7
                                                         7?. /   28/100
                                                                        22.
                                                  AVG. MOLECULAR

                                                  WT. DRY STACK GAS
                                                                         2g.
 VFT/AP4B
                                          137

-------
CL I ENT /*'- / ^ ^ / ~' <*''" ;*•'* ••*
PORT 10CATION / /<-"vv- Y ( ,/Yvc c ,/ A.\~ฑ.
DATE** A* ?v AMBIENT CONDITIONS / f S^f fฑ'"
OPFRATOR/S r1 V S'- /•*•*"* W
RUN NO. /-;
SAMPLE & ME
METER BOX C.
FILTER NO.
CLEAN-UP NO
BOX & PROBE
FER BOX NUM
>M A a
8ERS^/U< fc '>

, ... H K- 2-i-y- /
^ S - S ป TARE 3 '' *
VALENTINE FISH ER & TOMLINSON
SEATTLE. V/ASHINGTON
TRAVERSE SAMPLING DATA SHEET
ฃ j IMPORTANT: FILL IN ALL BLANKS
SCHEMATIC OF TR/ VERSE POINT LAYOUT
INSTANTANEOUS READINGS: RECORDED ป BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
'3- 2&/
-• 1 • ;
1 -7
/ ><7
•' /•* > ,

/ -i / .'
( /
H. /. -'• ,. •>
^

, • I
/ ' ' '
- • v
/ .'•';
' A -'ซ' '• J '->


, )




-TOTAL'/
AVERAGE
ELAP.
TIME
(MIN)
t>
(>>
C>
fj_
tฃ
/->
/' &
12 /
'M
:17
j <-•
*? '>
, _-7<; .
'>*->


T-'
>"/
S 7
( .O


	 _ ..
(*:
'///'•
DRY GAS METER
(CUBIC FEET)
ฃ*e-sT7:.?7
0O V. /
^/^ ฃ? , s.~
^'i'.', . 7:,'
^•v / 7 'i
irV^.H
fr / > r'""
C? / i " , =.Vc. 'i / V
P/^.xv
f^^.c> , t
fy t4/ • S"
Hf-1 •* :.i
o / . / ,
or- <•• •^•
(r'^i • C. (i
. .^
^r'5 cy
o', 6 .06 b


— — ..
-;, . .-; /
'//////
DRY GAS TEMP.
INLET
*?<->
9^
~~V-s"
c~fL> /^S
9B
/ซ1>C''
A> /
/o *i '!•<
x^ > >'
/o<-^
/'<9 V
/&f /faj

/(> f
1 1 ')//(;ฅ
I/O
St 1
ft 2.
1 1^



?',.v
OUTLET
&f~
& 1T
fc
&^'
a t'
& i>
& ฃ''••','
ฃ&
&'/
6"~\
7 V>o
c//

!i-2 /'I ?
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/H
*/^
*7 S


	
•s
% 'F-s-W, 'R
BOX
TEMP.
oc>7
^7^
,2 '?•*"
.?.•&'
.1 '>'•>
.5'1M7
J?c/?
.^•i::.'



	 	
/ // /
///,
IMPINGEIl
TEMP.
(•F)

^'C
~Vr-
*> •>
s:i_
^ r o
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TC
:Vtป
t"->0
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sr/
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^>o
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—
///x
^/X
•3
L
p
A
C
R
S
P
P
ARCMETRIC PRESSURE (P
FAK RATF ^x0 / CFM
ORT PRESSU
SN * PB *
SSUMEO KOI
FACTORS
EF.AP ,t
n) ' ' ' ' "H9
U' a
a -?''T "HG
HE (Ps) ^ "HoO - "Hg
PS ^ ^. - • ^ ._ "H9
STURE / ' '-' t MAX VH "H,O
n
y*> . o-^*./

TACK DIMENSIONSO'-l>/Oi/ AREA '^^ / O F2
ROBE NOZZLE niA ^--
ROBE LENGTH '?"' Nli
IN: AN - ฐ^'/ '^o f2
•1BFRA/ SIDE /
AVERAGE VALUES! READ WITHIN THE TIME INTERVAL
POINT
^ /
2.
9
-c/
2>_/
X,
-?
^
o
•J
^
^t
— i-


.

'///

PITOT VH
("H20)
.c;' /

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<^J
, o/ '?

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. r ^ / ?
, c v -^

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^ <:• / S~
,^/^r
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t'-'/V
• > ,' •>"
<:>/ 6
<9/S"
	


'////,
••///'•
ORIFICE AH
("H 0)
DESIRED
'~^tฃ "
*."{.'.
,'^-i
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. (
7

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. •/
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ACTUAL
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VFT/APlt

-------
                          VALENTINE, FISHER & TOMLINSON
                    STACK MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT
LOCAT ION
OPERATOR
            >/             r
          //ฃ c'*/s?-/_'. ^7  .-J x
                                                            RUN NO.
DATE
                                                                     NO.
                  -5
SAMPLE BOX
                  .'•€
H20 CONDENSED, ml (1 ml - 1 gm)
     BUBBLER (#1 W/APPROX.  100 ml  WATER)

     IMPINGER (.#2 W/APPROX.  100 ml WATER)

     BUBBLER (#3 DRY)
 H20 ABSORBED BY  SILICA  GEL, ml
 TOTAL H20  COLLECTED,  ml
 VOL.  OF H20 VAPOR @ 70ฐF.  AND 1 ATM.
 0.0474 x TOTAL H20
 MOISTURE IN STACK GAS,  %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT. OF STACK GAS
                                                  CONTAINER WEIGHTS  (gm)
                                           FINAL
                                                   - /
                                                            INITIAL
                                                         632.2.
          NET
                                                                       i* 7
 % MOISTURE IN STACK GAS = 100 x VOL. H20 VAPOR
                            VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY GAS = 100-% MOISTURE IN STACK GAS
                                     100
 MOLECULAR WT, OF STACK GAS = AVG. DRY MOL. WT. OF GAS X MOLE FRACTION +
                              18 X (1-MOLE FRACTION)
 VFT/AP3C
                                           139

-------
                          VALENTINE,  FISHER & TOMLINSON
                LABORATORY  ANALYSIS  AND TOTAL PARTICULATE  SHEET
CLIENT  ^ฃ-/P^)  /=/^ฃ?^SC :~	 DATE OF ANALYSIS  & -/,2- ~7 ~

EVALUATION LOCATION  X ^TV^x- ^ ~  /="/.>•>- ^-. X- c." -l"      RUN NO.   / ^~	

EVALUATION DATE     ฃ - / J: ~ x'.S""	 CLEAN-UP SET NO.    ^ ^? - ^—	
I.   EVAPORATION OF  // 6?        (ml)  OF
     RINSE & BRUSHING OF  NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.

          FINAL 772 ^ ~? P.. O'      (ing)

          -BLANK (( .OPS' 7  mg/ml)  (   // $?    ml) = ,-7    mg)       =   yj . c-    mg

II.  FILTER CATCH  /^^5^  //c'j S -'/  // _ (Media Type  & #)

          FINAL >3?6.fe    (mg)  -  TARE    3.5-^. / _  (mg)       -   "2.0 . 5~~  mg.
III. HYDROCARBON OBTAINED  BY  ETHER-CHLOROFORM EXTRACTION ON        " - "  '   —
     WATER IN IMPINGER AND BUBBLERS.

          FINAL 792.3 2.3  (mg)  - TARE   ~7ฐ)O / ^-. 8     (mg)

          -BLANK ( _ A  g _ mg)                            =  /g . 3 7,  mg.

IV.  PARTICULATE FROM EVAPORATION OF   -^ 5~& _ (ml) WATER
     IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
          FINAL ~?\a%&'-.7  (mg)  - TARE   7^ 7^ Q .7       (mg)

          -BLANK ((^o_2_8^_ mg/ml)  ( _ .Z g"g _ ml initial

          -   y^.J^  ml CONDENSED = Z3J".  ^o ml) = c,.~7  mg)    =   / 9 . 3  mg.

V.   PARTICULATE FROM  / / ฃ~ (ml)  OF  >9 C^TO / '/<ฃ"" RINS E OF IMPINGER,
     BUBBLERS, AND CONNECTORS AFTER FILTER:
          FINAL 7g7^y.2. (mg)  - TARE 7 ff7 <^. /        (mg)

          -BLANK ((> gcJr?  mg/ml) (  //^"  ml) =  g>  ^  mg)        =   / ^, f —  mg.

VI.  TOTAL PARTICULATE  =  I + II + III + IV + V                      =     ? % .7  mg .

     BLANKS      >S  K''-  ''
                                                                 FINAL  _ mg.
     ACETONE  = _ mg/ _ ml = _ mg/ml     TARE   _ mg.
     ETHER-CHLOROFORM = 	 mg.(FINAL 	 mg -  TARE
mg)
     WATER  = 	mg/	ml = 	mg/ml.   FINAL	 mg ,
                                                                 TARE	ng
VFT/AP9 A

-------
                     VALENTIN:,  FISKER & T^MLINSON
                   ORSAT  DATA AND CALCULAT r.ON SHEET
CLIENT
                                                              ~. •—' „>•
SAMPLING POINT LOCATION _


DATE  9//Z /7 i^    RUN NO ._


TIME OF SAMPLE COLLECTION
                             •*  v/>V:',•* •'
                                          HOW COLLECTED
TIME OF ANALYS IS
                                                             /V
                                                              .? . '
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + Q2 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
CO



N? (100-Above)
ANALYSIS
//I
o.i/
>
^y^
zฃa
W
-7


#1







ANALYSIS ANALYSIS
n #3
^'5 r:5^-
r^.f i J7/ o
J-A * \ Z/ o
t






ANALYSIS
#4
•^ -^'
-'J "-'
r^. rr




#2
<2-3
2&.(*
O



"79. /
#3
^, <
2c>. ฃ
C2



79
#4
a ^
2c?.r
O



79. /

AVG.
*f
zo.(?
o>



79. /
RATIO XwT./MOLE
MOLE WT\ (DRY)
44/100
32/100
t 23/100



28/100
AVG. MOLECULAR
./76
ฃ,ฃ92




2 •?./ฃ!
•5$ ->-
•*->./<-
                                                    WT.  DRY  STACK GAS
 VFT/AP4B
                                             141

-------
— -— - ^_r
CLIENT E :PA
PORT LOCATI
DATFf>' / 2
3N /?L'V/r rCri*S7>Wr ซ-
CLEAN-UP NO. ฃ/">.i Bl
BOX & PROBE HEATER SE^
ANKS A


VALENTINE FISHER & TOMLINSON
SEATTLE, WASHINGTON
TRAVERSE SAMPLING DATA SHEET
IMPORTANT: FILL IN ALL BLANKS

5 7ACt
•;^: ^ป*
•BAROMETRIC PRESSURE (P
LEAK RATF OJi c.FH
„) 2V 7^ -Hq

a . ^ S
"HG

PORT PRFSSURF (Pr) • ' "H-,0 • "Hg
PSN " Pfl + 3
ASSUMED KOI
C f ACTOR _A
REF.AP..^
?s ' ' ' ' "Hg
STUflF / t MAX VII "H.O
*
^1 .^W

J ^-26- o~ STACK DIMENSIONS' /' 'it AREA ' ' i. F2
SCHEMATIC OF TW VERSE POINT LAYOUT
INSTANTANEOUS READINGS: RECORDED 9 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
/•- : .'.7



//6 H<



/'• ,}<







•2^ALฑ>
i

,




—? — ;>-"/
/ /
.AVERAGE
ELAP.
TIME
(MIN)
^
^
<.-
4'7
SV
^1
-73
•**•>
4-B
v/
*'*y
^ -T
4 f


.

,
'///>
DRY GAS METER
(CUBIC FEET)
^"
v- "y,^ •?
^i^ J .
^•f O / I
ซ•/ o/ 67-
*/ ^ •> • ^ *>
9^4. v~s"
<7o< . c//
^!<~>''TifL

Vc'<7. 7
V// -1
cl/3 1
1' ? ">
ff."/> M
r^/ 6 • J S"'
?'7 5
'/ x^ ^
y/ v - c
.'LlL .ฃ_..V.O


. . ..._..
-? •/. i. ' h
'/////,
DRY GAS TEMP.
INLET
ฃ^
^•i-
-^
'7 '3-
~J?"
f^^/f*1
r 2
V 5
ฃ/7
9 6
.__'4_rf__
_

	
^^•>.'{
OUTLET
ฃ>%
<:• ^
 '*
ฃ-3 / fc/J
c-'v

frif'
e/
^'-i
.Jr_I^

	
/: , "_/._
7 / *F -*TV/'R
BOX
TEMP.
/92
•?/<*
iSL
jC.4o
~^T
.2s~o
IS
~^r
~i^~
I'fcO
-i^r-



	
////
'///,
IMPINGED
TEMP.
CF)
<:: <•
S'l
^>"o
^;
*>&
j"8
^.a
"7^-
-%'
*•/ ^?
s 'I
^•^f
i i-<
-v^'



	
'///
////
PROBE NOZZL
F niA / 2. IN: AM ' < / fl

PROBE LENGTH ^' NUMnFR^ SIDE ~
AVERAGE VALUES; READ WITHIN THE TIME INTERVAL
POINT
^ /

t$
^
A? /
•2.
1
2

^
J> 1
ฃ
.'^ 1
—1-



•' / /~
;;. .>
////

PI TOT VH
CH20)
^"fe^R~J"
. f
0/2
<)//
. i-X' ป 7
O / ^
. 0/5"
o / *V

iป //
o / ^
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ro<-
c^ /
c^ i 2
C1/ 1-
LX"i'/
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is
^
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6
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t^
^ j
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^^
• 66

S'
6-7



, , , ,
//.v-;H2o
.•,M-H20-.u./"Hg
Pro - PR +AH - " J. /-/- "Hg
PUMP
VACUUM
("HgGA)
' i S /
2..C

^ -O
/ • ^>"
*Z ' O

•'J . >
/. <(

-3 C

/-'J
/•S"
3..C
2 . Q
i ~?T~
/ , 7
o o


7— /- / —
'/// '
'///

STACK
TEKP.
CF)
_/7^

l?&
/ (~ • V
/ -iT
/C/O
/ -7-^
/7?>
/^?*TET-
y '7*^'
/^io
/'! o
/fic
/ C1/
/9 O
/P>'i~
/A-c-
/7o





' S
, l
/ #
-------
                          VALENTINE,  FISHER & TOMLiu.
                    STACK MOISTURE  CONTENT DATA AND CALCULATIONS
CLIENT  ฃ.  ฃ A .
                 RUN NO. /o
LOCATION Mr/, -r- vC ^ U tS.^  ฃ-ฃ.
                          NO.
OPERATOR  ^ ( C-!. 'XT f^  /
                 DATE
SAMPLE BOX   .-?
H20 CONDENSED, ml  (1  ml  =  1  gin)
     BUBBLER (tfl W/APPROX. 100 ml WATER)
     IMPINGER (n W/APPROX. 100 ml WATER)

     BUBBLER  (#3
 H20 ABSORBED BY SILICA GEL, ml
 TOTAL H20 COLLECTED, ml
 VOL. OF H20 VAPOR @ 70ฐF. AND 1 ATM. -
 0.0474 x TOTAL H2o
 MOISTURE IN STACK GAS, %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT. OF  STACK  GAS
                                                   CONTAINER WEIGHTS  (gin)
FINAL
INITIAL
                  r 7 /
                                                                        NE:
                            /.
                           / 3. "7
   MOISTURE  IN  STACK GAS  ป 100  x VOL.  H-^Q VAPOR
                             VOL. DRY GAS + VOL. WET GAS
  MOLE  FRACTION  OF  DRY GAS ป lQO-% MOISTURE IN STACK GAS
                                      100
  MOLECULAR WT.  OF STACK GAS =• AVG. DRY MOL. WT. OF GAS X MOLE FRACTION +
                               18 X (1-MOLE FRACTION)
                                    III
 VFT/AP3C
                                              143

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY  ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ฃ: /& Xj   /=•/•?ฃ: ^L.A  -^ _ DATE  OF  ANALYSIS   7- /
EVALUATION LOCATION  /-./--- . -.. —  /-"//-    •-:..-  -.—     RUN NO.  /
EVALUATION DATE    g - / f - -7 ^s-— _ CLEAN-UP  SET NO.     3 /- S
I.   EVAPORATION OF    // 2-      (ml) OF
     RINSE & BRUSHING OF  NOZZLE,  PROBE AND GLASSWARE  BEFORE
     FILTER.
          FINAL -J77CZL.3 (tag)  - TARE  "77^^.^. ^       (mg)

          -BLANK (( . c?gf 7  mg/ml) ( / / 2     ml) =  .  &   mg)           ฃ . 3      mg

II.  FILTER CATCH  SJ 6>A   / /     (ml)  OF  ACETgtJt — RINSE OF  IMPINGER,
     BUBBLERS, AND  CONNECTORS AFTER FILTER:
          FINAL 7"7//ฃ/.
-------
                     VALENTINE,  FISHER & TOMLINSON
                   ORSAT DATA AND  CALCULATION SHEET
CLIENT  /T, P, A.
SAMPLING POINT LOCATION

DATE  ^X/? ^     RUN  NO.   /6
                                          HOW COLLECTED 6*34^3
TIME OF SAMPLE COLLECTION  /
-------
VALENTINE FISHER & TOML1NSON
CLIENT ฃ /ฐ /-I /:~'J.'ef).'\ce
PORT LOCATION J-ht^e YC-H"L'<- /V AV^S <"i ~V/0_T A-
nATEr* / ? -^"AMBIENT CONDITIONS < ^ ->'^ 7^"
OPfRATOR/S X^d-^^/Cb -^ S/"/ป/V7t/V
BUN NO. ' 7
SAMPLE & ME1
METER BOX ฃ
FILTER NO.
CLEAN-UP NO
BOX & PROBE
FER BOX HUM
,H /• Rl
RFRS^X'i.- i
0.
.i?> ^"TARE /fcr, / M
f pi ANKS &
HFATfR SPTTINC, -^-TO^i .?(D%
SEATTLE, WASHINGTON
xTy/VW/V TRAVERSE SAMPLING DATA SHEET
IMPORTANT: FILL IN ALL BLANKS
S"-W /^^
'BAROMETRIC PRESSURE (P
LEAK RATE _^-Q2__CFM
P
A
C
R
ORT PRESSU
SN - PB *
SSUMED KOI
FACTOR *

:r . A P
RE (PSU-L
ps ;.' •'
n)^V 7^.i "Hg
a .2'-i'**~ "Hf.
"HoO - "Hq
;, /-•' "Ha
STURE / -i MAX VII ~Hnn
2

STACK DIMENSIONS ^^-r'!. AREA /-/7^ f2
SCHEMATIC OF TR/ VERSE POINT LAYOUT
INSTANTANEOUS READINGS: RECORDED 9 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
($ 4 ^











' i












/TOT/U//,
, AVERAGE
ELAP.
TIME
(MIN)
0
J2/t
•>"
7Xz.
1 ^
/ 2Yt
. <• —
-^-
•j-21/i
3~>~
;nYt
Vc •












'^>
//7//
DRY GAS METER
(CUBIC FEET)
9--?/ V-2 ^

^7 i'2 (.^5
^2^-.2l.
5'?^ ^'C/

'/•?? 70
f/^ i. /*^
^ ^ ^ -y 2 s'
•/ Z 5 4 ฃ
72 5 ^^;
C Z-H • /OS"
V ^ */ • ^ -1 ^












.'../)/
'//////
DRY GAS TEMP.
INLET
7ฃ>.
7€H.
'7 V-
'•7ct
fr"t >
P c>
f /
^ /
^ <:
G'S
&*!
&
7^,
T>*
•76i
/ 6.
/'fe
-77
*j&
~7 V
^4 c^
-#s-
f? i^












A ./ .:.
/-; 'F-,;.j'rR
BOX
TEMP.
^2.->iT
i<^/
~fes~S"
j2-io
3 oc
Al^T
-^•^i"
(2^"^
J?fiO
5-t-O "
^f












'///
'//,
IMPINGED
TEMP.
CF)

'72
i'o
Y/

•srfej
i;
-*&?'
*a fi




	






///
'///
PROBE NOZZLE niA />>
PROBE LENGTH ri" NU
IN: AN -••'•., -P2

AVERAGE VALUES! READ WITHIN THE TIME INTERVAL
POINT
C- 5
;>
,
.<
'.

//
,
,
•/










	

'~/~s~.
/
'///

PI TOT VH
("H20)
'e~~7tt~*'
o / 0
,OC6
__, ซW ฃL
• o/A
o / s~"
• o / ^T"
.c;/ 9
O}S
O/^
• ( V ^
^ ^ fa











-ry-jr-/".
'////.
/////
ORIFICE AH
("H 0)
DESIRED





















	

•y / /
//X/
ACTUAL

, , ป •,
/"sT

.OS"
.tX^s""
ซ:><:/<,"
— %.
~^M
rfrf'i
c^/








	

, , y /
- V.^"20
t ) * J fl?^ xL Ort '
Pm - PB *AM - ;' ••). 7 ? if "Hg
PUMP
VACUUM
("Hg GA)

*5~ 
fi~' O

JS". 0
S"/C3
"a" 0
6" - O
'i". O
'J , C>
5"-f
•i.'" &
5"~/ o








- 	 	
• 	 ••
///•
'///.

STACK
TEMP.
CF)
OPACITY
OR
XC02
^ . • .r .

i? 2x"
J?ic
i.xo
^(1Cj
/ ?r~
/^'o
/8o
/ ^^ /
x *L^ i
/&c-
-~/Z.z~
y 77




,






-
i . )
/ ;ti
.;•' o ^ "R























X" •




-------
                          VALENTINfcl, t'lbHER * T
                    STACK MOISTURE CONTENT DATA AND  CALCULATIONS
CLIENT
                                                             RUN NO.   /7
LOCATION

OPERATOR
                                                                      NO.
                                                             DATE
SAMPLE BOX
H20 CONDENSED, ml  (1 ml - 1 gm)
     BUBBLER (II W/APPROX. "100 mi WATER)
                                                   CONTAINER WEIGHTS (gm)
                                            FINAL
                                                             INITIAL
                                                              2  i-
                                                             -=•//./
     IMPINGER (tf2 W/APPROX. 100 ml WATER)

     BUBBLER (W DRY)


 H00 ABSORBED BY  SILICA GEL,  ml
 TOTAL H20 COLLECTED, ml
 VOL. OF H,0 VAPOR @ 708F. AND 1 ATM. -
 0.0474 x TOTAL H20


 MOISTURE IN STACK GAS, 2


 MOLE FRACTION OF DRY GAS


 MOLECULAR WT. OF STACK GAS
 X MOISTURE IN STACK GAS -  100  x VOL.  H^Q  VAfrOR
                            VOL. DRY GAS + VOL.  WET  GAS
 MOLE FRACTION OF DRY  GAS  -  IQO-*  MOISTURE IN  STACK CAS
                                      100
  MOLECULAR WT. OF  STACK GAS  -  AVG,  DRY  MOL,  WT.  OF GAS X MOLE FRACTION  t
                               18  X  (1-MOLE FRACTION)
NET
                                                                      — O.
                                                                       /. 2.37
 VFT/AP3C
                                            147

-------
CLIENT
                              X- / /e•ฃ=•
PORT I OCATION
DATE ^-/-S/X
                                        '•/
                             coNomoNs
RUN NO. __/_ฃ__
SAMPLE & METER BOX
METER BOX  AH      /.'.
FILTER NO. '•>  V--'    0 TARE
                                                        VALENTINE FISHER & TOMLINSON
                                                             SEATTLE, WASHINGTON
                                                            TRAVERSE SAMPLING DATA SHEET
                                                           IMPORTANT;   FILL IN ALL BLANKS
                                                                                        *ฃ.
                                              _mg
.; BLANKS.
        CLEAN-UP NO.
        BOX & PROBE HEATER SFTTING 3L~
                                                                                            //
                                                             Q  O    O    O   O
'BAROMETRIC PRESSURE
 LEAK RATF. :'j*~-   TFM 
-------
                          VALENTINE,  FISHER  & TOMLINSON
                    STACK. MOISTURE CONTENT DATA  AND CALCULATIONS
CLIENT
                                                           RUN NO.   /
LOCATION
OPERATOR
                                                                          83- 5
                                                           DATE
SAMPLE BOX
                                                  CONTAINER WEIGHTS  (gin)
                                           FINAL
                                                            INITIAL
                                                          3 *#.
H20 CONDENSED,  ml  (1  ml  =  1  gm)
     BUBBLER  (#1 W/APPROX. "100 mi WATER)

     IMPINGER (^2 W/APPROX. 100 ml WATER)

     BUBBLER  (*3. DRY)
 H20 ABSORBED BY SILICA GEL, ml
 TOTAL U20  COLLECTED, ml


 VOL.  OF H20 VAPOR  @  70ฐF. AND 1 ATM. -
 0.047A x TOTAL H2o


 MOISTURE IN STACK  GAS,  %


 MOLE FRACTION OF DRY GAS


 MOLECULAR WT. OF STACK GAS
 35 MOISTURE IN STACK GAS - 100 x VOL.  H^O  VAPOR
                            VOL. DRY GAS + VOL.  WET GAS
 MOLE FRACTION OF DRY GAS - 1QO-X MOISTURE IN  STACK CAS
                                     100
 MOLECULAR WT. OF STACK GAS - AVG.  DRY MOL.  WT.  OF  GAS X MOLE FRACTION
                              18 X (1-MOLE FRACTION)
NET
                                                                         6
 VFT/AP3C
                                        149

-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT  ฃj /a X=  /- /.**:-7 s z, /-' -. ~T	 DATE  OF ANALYSIS  >P-y ? -"7.5"

EVALUATION LOCATION  A / ^.- -  T.-1"   /=•>.-=ป•"  ^  -;-  -.7      RUN NO.   /Q	

EVALUATION DATE    ฃ*-/.?- 7i	              CLEAN-UP  SET NO.  ฃ ? — --—
I.   EVAPORATION OF    "? 7 _ (ml) OF
     RINSE & BRUSHING  OF  NOZZLE,  PROBE AND GLASSWARE  BEFORE
     FILTER.

          FINAL 7^7jf //' (mg)  -  TARE 1^ 7 7 5~. g _ (mg)

          -BLANK (( .caoS"  7  mg/ml)  (   "77   ml) =  •  <*f-  mg)           ^ ^L    mg

II.  FILTER CATCH  X'-/<^-'   //^y ^5 .-?'  // _ (Media Type  &  #)

          FINAL 3 3 7. ฃ> (mg)  -  TARE  35~/. 4 _  (mg)       =   3 S~* -^    mg.
III. HYDROCARBON OBTAINED  BY  ETHER-CHLOROFORM EXTRACTION  ON
     WATER IN IMPINGER AND BUBBLERS.
          FINAL   9J5g.^ (mg)  - TARE   ^3 7 S, 2- _ (mg)

          -BLANK  (    "^ & _ mg)                           =  /3> ^    mg

IV.  PARTICULATE  FROM EVAPORATION OF   3 J? .5 —     (ml)  WATER
     IN IMPINGER  AND BUBBLERS  FOLLOWING EXTRACTION  -
          FINAL   k73^J"~(nig)  - TARE  "7^ "7 //.V _ (mg)

          -BLANK (( .CQ2.5*.  mg/ml)  (     32. 5^      ml  initial

                   ^    ml  CONDENSED = ^?^ 8.*^ ml) =   . ^  mg)    =             mg
V.   PARTICULATE FROM  / ^-O   (al)  OF  ACฃ~7&f/E~  RINSE OF IMPINGER,
     BUBBLERS, AND CONNECTORS  AFTER FILTER:
VI.
FINAL '7Z2.U
-BLANK ((.0057
TOTAL PARTICULATE =
BLANKS. y^n ^-/
ACETONE =
ETHER-CHLOROFORM =
WATER =
2 (mg) - TARE 7 ^2.^-2.. 3
mg/ml) ( /ซฃ<2 ml) = ป ,
I + II + III 4- IV + V
mg/ ml =
mg.( FINAL
mg/ ml =
(mg)
3 mg)
mg/ml
mg -
mg/ml .
VFT/AP9 A

_
FINAL
TARE
TARE
FINAL
TARE

2^O, / mg.
^/ " . r~ mg .
rag.
mg.
mg)
mg .
me.


-------
                    VALENTINE, FISHER & TOMLINSON
                  ORSAT DATA AND CALCULATION SHEET
CLIENT ฃ"• P. A .

SAMPLING POINT LOCATION

DATE   0 Xi /~>C   RUN NO.   /
                                        HOW COLLECTED
TIME OF SAMPLE COLLECTION
                                         TIME OF ANALYSIS
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C0ฃ
02
ANALYSIS
#1
JL -i
20. f
ANALYSIS
#2
<•
-------
CLIENT ฃ(JA t I'.'fiX/i t-
PORT LOCATI
DATE <*•' 1 '-'' "'
ON H1-''iE->'ti-V..'k^.rl k'rs-
V AMBIENT CONDITIONS. ^^ O-0*.'-^
iDCOATAD/C ^-\( ( % M*^( li / > ^*"~ '-V f^* .> C. i -J
RUN NO. H
SAMPLE & ME
METER BOX ฃ
FILTER NO."
CLEAN-UP NO
BOX ft PROBE
FER BOX NW
iH /,-ฃ
BERs^t-K 4 'S


; HIANK<: A
HFATFR SFTTINP, ft
•'.'d-i"
VALENTINE FISHER & TOMLINSON
SEATTLE, WASHINGTON
TRAVERSE SAMPLING DATA SHEET
IMPORTANT: F!LL IN ALL BLANKS
-— ,
/vt> o ^|V>* / 1 ; 5J 
. f'

••' /,/ •
' !••<, ฃ&
j ' -> ><.

' -' ! 1
.' '

•'•' -•< //,'
/ . •


-l^'l.'
'

/.' > i




/TOTAL' /
AVERAGE
ELAP.
TIME
(MIN)
O
\'
_ฃ.
9

/ -T
/f-
5 /
."> /•
."7
!ซ.
'>' ">
, ,\>
-; /
•/ 2
'/*
vf
•A i
:. y
.;"-?
^ ,_"




S' 7
'////
DRY GAS METER
(CUBIC FEET)
•y c,K 72 2.
c/\ V- ^"-i

J?' 6 _'.(.-
^ C- f> i.- /
9 L- > *•• '-
'//•' '.' , / 7 ,;

c< p ^1 , •? Y
'•
'/////s
DRY GAS TEMP.
CF)
INLET
^•'c/
*'-<:-
^' */
72
7-3_/v
~~$*r~
h^/tf
ฃ7 /ft
ฃ
-7s
'/fc
TT
'&/ '/S
1 1
s
"^x-
'7/u
._iZL.




/ / / \
/ / /
IMPINGE <
TEMP.
'7<.
-/"2
7 i
^y o
f^"
'/C
=^:
~~$Z~
^
~it^
^(0
-/o
-^t:-





///
x//;
'BAROMETRIC PRESSURE (P
LEAK RATF /• ^ CFM
Q) ^ A >'- ' "Hg
a '> '> " "HG

PORT PRFSSURF (Pr\ > "HoO - "Ha
PSN ' P8 *
ASSUMED KOI
C FACTOR _/_
REF.AP > '
PS ••' V. .' ' "Hq
STURE '1 ซ MAX VII "M.O
A.
Q 1
'>C- ,-// 'ปc> . ^< -

5TACK DIMENSIONS ''/•/•/', *AREA / . '• ' f2
PROBE NOZZLE niA Y>
PROBE LENGTH "'' ' Ml)
IN: AN • ;< p2
•1QFR / SIOE.^^ 	
AVERAGE VALUES'.READ WITHIN THE TIME INTERVAL
POINT
A !
/I
1
-^T
~t
7

r /
4
. /
^/
7~) /
	 2.

— i



f s
~ฑo
////

PITOT VH
CH20)
^ i ' ;' / fr
C'ซ-"'<-
-• v. (•

 \ I
. <->'•*-(
< ; S -\
.(-'i ~\
^ ( '•>
. '^ 1 S
. C f .'

. r \ t-

> .^-
•Ji^?
'/ <^-
S.-?
I.I
I / i
/. ^
. < •• "7
/
/.ซ.'/
/• ฐ
, ?6
. /C
_ ^:
r'
• ^'f
, ^ >
. '/ f-




•T-r-T
////
ACTUAL

~""v^~
• ;•'>
/' /
/ • '>
/ ^
.C'j
. 7
/ • •- 1
/'(.'
'76
V c-
. ^,-
• ^
- '-'- /
- ^' ?
V '




r-r-,-,
/-/•o"H20
.')L "M20".(%-Hg
Pm • Pa *AH - /' 'X-'j .'•.' "H9
PUMP
VACUUM
("Hg GA)
' — '/ /'', ' '
/ "7
--/-.-•'
'"/. '-'
;> . /
^' C'
•j". c-'
'i -''
_> •• :
•? .. •
'/ -^
• / ." (
^ ^-.
•:; /'
'/ป ('
*'' • 1
S **
/s.
/7.c
.''.-• .^'


.-_ ....
S f ,r
/// '
// /.

STACK
TEMP.
CF)
-
^' ^'/ S.
o / •-/

? / vi"
.'' ' 'ป
:'>&('
j K ->
/ *•
T> -. 7
v U-
'-i V >
•,'.''c-
-'.:;•: T-
^ * 1 S
'•' '•>
:'/s
* * > v^
0 - /^I
4> ,; -^

.



' '
-1M )
^ /
V/ 7 ฐR
OPACITY
OR

























S


( >/r--
f J
c- V
C'.i'
C V
•Oe:
, O^i
. C- '. '
,0lฃ
^( C-
'^ i '-V
c-iซ
<.-• —
. o ^
-t'i-7
err
. 0 ' fc
.IJIC
, (.- > '2

-------
                          VALENTINE,  FISH I-,,-' & '1OMI.1NSON
                    STACK MOibTURE CONTENT DATA AND CALCULATIONS
CLIENT
                                                             RUN NO.  / ml WATER)

     BUBBLER (i:3 DRY)


H ,0  ABSORBED  BY  SILICA GEL,  in I
 TOTAL H20 COLLECTED, ml
 Vl-L.  OF H.,0 VAPOK @ 70ฐF. AND 1 ATM.  -
 0.0474 x tOTAL H20
 MOISTURE IN STACK GAS, %
 MOLE FRACTION OF DRY GAS
 MOLECULAR WT. OF STACK GAS
                                                                       NO
                                                              DATE
                                                   CONTAINER WEIGHTS (gin)
                                            i-'INAL
                                                 r9,3
                                             4?*. S
                                                              INITIAL
                                                                 ฃT
                                                                        NET
                                                                         4,
 % MOISTURE IN STACK GAS  -  100  x VOL.  11-jO VAPOR
                             VOL. DRY GAS + VOL. WET GAS
 MOLE FRACTION OF  DRY  GAS  =  100-% MOISTURE IN STACK GAS
                                      100
 MOLECULAR WT.  Or  STACK <.Atป - AVG. DRY M-/- .  WV. >"' CAS X  SOLE  t'KACTlON
                               '. 8 X (i-Mo-:-. cRA  ^-jtt)
   L7AP3C

-------
                         VALENTINE,  FISHER & TOMLINSON
                LABORATORY ANALYSIS  AND  TOTAL PARTICULATE SHEET
CLIENT  ZT /ฐ /4 /- /** ฃ.- P<^~ /" //-^T-V../-,. .="         RUN NO.    / ^
EVALUATION DATE    S - / ฐ)-  ?~CLEAN-UP SET NO.
I.   EVAPORATION OF    / 6 g?      (ml)  OF
     RINSE & BRUSHING OF NOZZLE, PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL •79^-g?  ml)  =  . ^    mg)      =    / &       mg.

II.  FILTER CATCH A?,5X?  //ฃ?Jj /.j//'   // _ (Media Type & #)
          FINAL  40 7* G  (mg) - TARE     Jog. /        (mg)      =    33
               /77, 5-   ^.         /76,^
III. HYDROCARBON OBTAINED  BY ETHER-CHLOROFORM 'EXTRACTION ON
     WATER IN LMPINGER AND BUBBLERS.
          FINAL  •?(*ฃ* Q~*& (mg) - TARE   ~?L ฃ, 0 A /       (mg)

          -BLANK (     /•  8 _ mg)                           =      2-   ml CONDENSED =  ^ / >?. g   ml)  =  . 
APFTONF - mp/ ml -

ETHER-CHLOROFORM = mg.( FINAL
WATER = mg/ ml =
VFT/AP9 A
3.*? (mg)
= • ง mg) = x <^. P
= d^.-^
FINAL
mg/ml TARE
rng - TARE
mg/ml . FINAL
TARE

mg.
mg,
mg.
mg.

mg .
rag.


-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT

SAMPLING POINT LOCATION

DATE AU&. /  /fjf RUN NO._/2.
HOW COLLECTED
TIME OF SAMPLE COLLECTION
TIME OF ANALYSIS At/&.
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO




COMPONENT
% BY VOL. (DRY)
C02
02
ANALYSIS
#1
-
ANALYSIS
#2
<^. 2^
2.Q.4
2.0. <4



ANALYSIS
#3
C7. 3
^af
2or<3
ANALYSIS
#4




•



K
o > "^
7.0. 2.
O



7 ,\
1
o


1
1
1

77' ฃ



AVG.
0,235
Zo,/67
O



77'4
RATIO \WT./MOLE
MOLE WT\ (DRY)
44/100
- /o3
32/100 '}ฃ,ฃ&
2a/ioo



28/100
AVG. MOLECULAR
o



22-2^
2asi
                                                  WT. DRY STACK GAS
 VFT/AP4B
                                     cr;

-------
CLIENT  A'/?-I    X.
PORT LOCATION
DATE-  f'-
OPERATOR/S
RUN NO.	
                          !
PORT PRESSURE (Ps)
•"•CM " PB + ps
bN ฐ J
ASSUMED MOISTURE
C FACTOR /,ฃS
F (pn) ;•",.*•-•.
1 U'
TFM ra 7--'
' "Hod -

~ t MAX VH

"Hg
"HG
"Hg
"Hg
"H20

REF.AP . 0'-(-
F1ITFR NO. -7-2- T ** TARE' ' "V7/. •> AREA / > /. / pZ
CLEAN-UP NO.A/-^ -t BLANKS A PROBE N077I E DIA.X^ IN; AN ' >• F2
BOX 4 PROBE HEATER SETTING '<"ป-' & ;' /" SCHEMATIC OF TRAVERSE POINT LAYOUT PROBE LENGTH >" Ni!MBER_ฃ7_ SIDE 7
INSTANTANEOUS READINGS: RECORDED 8 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
/4-/<>
/_/_/ z.
/ / -/ )
> t •-, /
!.:• ~''H -"V
•' •/ L, t-
/ ''/'_, J
/ '. ', y
• . -•/>' l'-'
-, /
' '.
•' '. ; "'
•' ' i~ ti.
i\
i e
| L?
->--•'•, 2t


.- ::. -' •->
vrii

TOTAL
/- • ' /
AVERAGE
ELAP.
TIME
(MIN)
O

.v _ .
-7
.6-
^
/o
/^
/Y . .
/6
/f
^ C "*
rt i'^
•'•/
-C
v^r
>(
^
"^'l
n
•V
%••

7 ^

X/ .' ' /
DRY GAS METER

(CUBIC FEET)
c -^ ฃC s
ฃ <* x T <" i
/*" 
V,AO".
""/""/ 2 . <^. "^
c/lr> ^;V
5" '/ v x 2
.t/'/^-'-/.^. .
•r/V>' c' 7
c^ /c '^<ป
-/'/ 7 7o
c<-;t- tซ
'"' '/ i • t. (
r ^ vc . (.• <: ^
f, '>'/


	 ,.cl


/r>< .3 •/

/ / / / / /
DRY GAS TEMP.
(ฐF)
INLET
72
' *t
?(..••
~7*~-
"/ V ^? '/
??<•'
— '/
<-• -/
^ //f . /
O i
fr'ei
.•c/t'.,
/ // <+
^.i 2
((. '<
'{ "^
S't/'-J-V
ฐi S"
<->
1
9f
- -
2 ASM
OUTLET
r r
C: ป t
* f
r
^' '
(:C(
4V./6'/
7c-
,YC
I*—/
'7 //?/
72
.!7.^
/ i
'*f.L.~f1
7**
''-'•ป
7?
7?/V"

.
?.'.? '
A-:'.

	
/ •• *J ,_

 " > <^r
^ L-r_Z.
Z" ป^
-^ >^.
'?•*-&.
2 •'( S
2 rt
2-'f^
'?<>.2
2 SC'
2<>o
- sl>
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7-V.V
7. VV
^ ) 7
~^~~
c'G^1
___ 	
_..^t?ฃl..
J *j O
	 . 	



y//

XXX-
IMPINGER
TEMP.
(ฐF)
'i'-j
Lf -
4i—
..j .?.
.^(.?. .
/:l;'?--
•\^.
flT._
^s
.rvfJ
^il 7
"t'^
*( /
^ .c'_
...$.ซ...
. .:Vt-.__
*D'O
.._„__

*• •ป**-'
. 	 	
	 -—. —
-( ""ป
	 	


	
///

/ / /
AVERAGE VALUES. READ WITHIN THE TIME INTERVAL
POINT


A"
t.
*->
_
/? /
T
7
'/
^
3""
•i
4 	
o /

— -
— xi"
"~r i
1— '
_j
-
7
__d_.
	
v *
XXX
XXX

PITOT VH

(MH20)
•^^-'-^
. t;- W
0 1^,
. f i(_-
.> / /
' o / •>
.. j
"• ' /
 S"

. 77
. //"
i- ('
• ^

...-kl.
.--tllS 	
f *
t-t:
— ^i'.i:


-s-r-r-
////
0)
ACTUAL
x.v y y
1
n
-t:
T •ป
-- 7 7-

, <
•'-
\-^-
- 77
,11
,t'
- 6 ^i
"y.- "~
• - -•-.-._ 	
, . Vi_ _
	 L.Zi..
•i 'i
.(•c-
. 	 !Ji_:L_

..
/./;HH20

.~)p "H20 "^ i, ; ^ "Hg
PUMP
VACUUM
("Hg GA)
2 '. ^
~> t
'.> 2.
> i
"? ^
^ '-•
S'. c
*•><•>
> ^- '
d .c-

E . L •
t • S'
/ C?


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' ' S
?.c-
	 LL_." —


/

'XX- x^

STACK
TEMP.
(ฐF )
' /, ( ^
..'I """
'•" J ->
'S ~>^
7 '-' • '/

•> •;
'7..--
? / 7

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—
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--
—


	
	
^.^_-7_7




                                                                                                                                                      .c/7
                                                                                                                                                       . 0/6
                                                                                                                                                      • CM!."

-------
                           VALENTINE,  i-'JSHEiv & TOMJJNSON
                     STACK. MOISTURE  CONTENT !)ATA AND '' VLCULATIONS
CLIENT
LOCATION
OPERATOR
           ,#ฃ&
-------
                          VALENTINE, FISHER & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT <ฃ/^/Z  /Os*rr,*=>^_/•- .•::. .^	 DATE  OF ANALYSIS   &-2&- 75

EVALUATION LOCATION  X? l/g/^ X9 ^ ฃ~  /="//* - 7 3            CLEAN-UP  SET NO.    	(ml) OF
     RINSE & BRUSHING  OF  NOZZLE,  PROBE AND GLASSWARE  BEFORE
     FILTER.
          FINAL Xfrgtf-y.T (mg)  - TARE  ~ฃ S^ **>.•(&	(mg)

          -BLANK ((• PCS 7 mg/ml) ( /5"JT"  ml) =  • ^    mg)            /o * *7    mg,

II.  FILTER CATCH  A: ^ ^  /.-c.^; /g. >/   //	  (Media Type & //)

          FINAL 2'~/. 3    (mg)  - TARE  3 S~C. ฃ,	 (mg)       =    ' /. 2-    mg,
III. HYDROCARBON OBTAINED  BY ETHER-CHLOROFORM EXTRACTION ON               *~       -
     WATER IN IMPINGER AND BUBBLERS.

          FINAL777,225~(ing)  - TARE   777/c5f gf      (mg)

          -BLANK (     A  B	mg)                           =    6. ^      mg,

IV.  PARTICULATE FROM EVAPORATION OF   .2 2 O	(ml)  WATER
     IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION  -
          FINAL  7^2ffg.6 (mg)  - TARE  ~7*) Z-7 ^jj       (mg)

          -BLANK ((. 002. 8 ^  mg/ml) (     ZJ5 &	 ml  initial

          -     //' B   ml  CONDENSED =  .2/ff1. <^  ml)  =  ซ  ฃ    mg)   =     cf. <=ป    mg,
V.   PARTICULATE FROM /_^ ^   C^1)  OF ^ Cฃ- T&sJiT RINSE OF  IMPINGER,
     BUBBLERS, AND CONNECTORS  AFTER FILTER:

          FINAL  *7ฃฃQ7.2.(mg) - TARE  7Cf^^3Qt~T'     (mg)

          -BLANK ((- QQS ? mg/ml) (  /3s?  ml) =   . Q   mg)        =   ^7. ^     mg

VI.  TOTAL PARTICULATE  =  I  + II + III + IV + V                      =
                                                                              .ฃ	 mg,

     BLANKS' €f/z ^^
                                                                 FI^'AL 	mg.
     ACETONE  = 	 mg/	ml = 	mg/ml    TARE               mg.

     ETHER-CHLOROFORM = 	 mg.(FINAL 	 mg  -   TARE               mg)
     WATER  = 	mg/	ml = 	mg/ml.  FINAL 	 mg
                                                                 TARE  	     mg
VFT/AP9 A

-------
                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
SAMPLING POINT LOCATION

DATE/teg. /  1415' RUN NO .  Z.O
HOW COLLECTED
/
TIME OF SAMPLE
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO



COLLECTI01
ANALYSIS
#1
0.2-
2jfi.?>
2.0.$
* TIME OF ANALYSIS
ANALYSIS ANALYSIS
#2 #3
0.2-
0.2.
Ztf.3 2.aj
20.3 2c?,3
'

ANALYSIS
#4 _,




1



I
COMPONENT
% BY VOL. (DRY)
C02
#1
#2
#3
#4
.2_ . > . ^_
i
02 -2,0 ซ /
<~T\ '• S*l fl
UU • ^J t ^-J

\

N? (100-Above)
77-9
2.0, i
*™*i 1
c. 
-------
CLIENT  t~ /'si  ^
PORT LOCATION //.*'*/-
DATE/-'- /ri VyAMBIENT CONDITION$rJXi_U
OPERATOR/S A' . •-. ^<'Q /'>'•
 TRAVERSE  SAMPLING  DATA SHEET
IMPORTANT;  FILL IN ALL BLANKS
                   lew  no/
BAKUnt|KlC PRESSURE IPB)  -- -1 •
LEAK RATE   -c *	CFM ^' 4 mg
I. ; BLANKS A
HFATFR SFTTING A
S"iAปn ic^ 1';^'= ASSUMED MOISTURE ^ % MAX VH MH,O
i" tf'/6 "^ R
FACTOR /

EF. AP <; H ,cl ^M '-^'1-
i *# n '.• o'i STACK DIMEN
/O* LC^T e> &„,<>* PROBE NOZZL
SCHEMATIC OF TRAVERSE POINT LAYOUT PROBE LENGT
INSTANTANEOUS READINGS: RECORDED 0 BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 MRS)
/(-•• >CI
' / ' V
TOTAL
AVERAGE
ELAP.
TIME
(MIN)
d
:>\-
/c-
: -'C '
.i -- >;-
i V/a
<: / / Vi
v J / 1.
•'.(•)
/ / / '''
DRY GAS METER
(CUBIC FEET)
,-, c-^.o 7o
/"/ Vr 	
/"I 2 i
?-' 0

-v /, ";
'//////
DRY GAS TEMP.
INLET
ฃ>'$
^Jfj^i
^t^
. *
ฃl '^
^i 7
/cc-
/c ^^^
/Cl
10 ^
:^ i-/^
OUTLET
ฃ.<•>
rf
77
* ^^1
• X*
VM
C^ C*
(Pt * '

	
;^>/^)
<3 ~7 ฐF -ซr^ 7 *R
i.J / j / / "
BOX
TEMP.
27o
•2 os
"v.!< T/
7 'V >
- -7*i


	 	
/ / /
///,
IMPINGER
TEMP.
4z
^O
.-do
-'/tp
^/ O
^ / o
'79
:)c'


	

////
SIONS^l^
E DIA.^
1 / AREA ' ' V • ' F^
IN: Aw ' 
"Ff"
•7
7
-7

,-s-s-.
•^.o
'///

PITOT VH
(BH20)
/'/?//
.cr-.-y
..•5' ซ >
.",.c> j'^
' 0 I
- < ^
. "."^oj 1
-~"r "
^072.
^_>i '-i
,C 1 ^



- ^.y.
'////,
'/////
ORIFICE A H
("H 0)
DESIRED
/ / S J-
^ -^v
"_"~7.3."
7?
6 '••
.(=<^
- Ci ฃ3
— . 	

-r-r-s-
////
ACTUAL
/ / y /
•x.-
:*
• S /
7 4
. „:_ฃ;< i
- ~ -v
c^-


- •-
/^.ซv"H20
J,, !"H20 -„,;•; "Hg
PM • PB +AH - .7 ; // "Hg
PUMP
VACUUM
("Hg GA)
/ / / /

S . c
< y\
/o . *-•


///
'// , ',

STACK
TEMP.
V ' •/
' ' > j
2 /">
?:,/ —
•vj '">."*'
v-b


_^_ T.._7 	 ,,
y -^ rf^
./ / e;
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OR
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                                                                                                                                                      o J V'
                                                                                                                                                       ciV
                                                                                                                                                       /.rfit
                                                                                                                                                       o/c
                                                                                                                                                       c.r
                                                                                                                                                        c-/7
                                                                                                                                                        o(t
                                                                                                                                                       .017
                                                                                                                                             VFT/AP1E

-------
                          VALENTINE, FISHER  &  T0MJ-INSON
                    STACK. MOISTURE CONTENT DATA AND CALCULATIONS
CLIENT
LOCATION
OPERATOR
                                      -VV
RUN NO.
DATE
         NO.
SAMPLE ZQY.
                                                   CONTAINER WEIGHTS (gin)
                                            FINAL
INITIAL
    CONDENSED, ml  (1 ml =  1  gm)
     BUBBLER (//I W/APPROX. 100 ml WATER)

     IMPINGER (1t2 W/APPROX. 100 ml WATER)

     BUBBLER (03 DRY)


 H00 ABSORBED BY SILICA GEL,  ml
  ^


 TOTAL H20 COLLECTED, ml


 VOL. OF H20 VAPOR @ 70ฐF. AND 1 ATM. ป
 0.0474 x TOTAL H2o


 MOISTURE IN STACK GAS, %


 MOLE FRACTION OF DRY GAS


 MOLECULAR WT. OF STACK GAS
 % MOISTURE IN STACK GAS ซ  100  x  VOL.  H^Q VAPOR
                             VOL.  DRY GAS + VOL. WET GAS
 MOLE FRACTION OF DRY  GAS  =  100-% MOISTURE IN STACK GAS
                                      100
  MOLECULAR WT.  OF  STACK GAS  = AVG.  DRY MOL.  WT.  OF GAS X MOLE FRACTION +
                               18 X  (1-MOLE FRACTION.)
NET
 VFT/APJC
                                           161

-------
                         VALENTINE, FISHER  &  TOMLINSON
                LABORATORY ANALYSIS AND TOTAL PARTICULATE SHEET
CLIENT
                        /ฃ
EVALUATION LOCATION _

EVALUATION DATE   g - / -^ -  7 ~
                                                 DATE OF ANALYSIS  2 - 2 -j,

                                       /~ /f* ~ .^.L ฃ .; ^     RUN NO.    2. /
                                               CLEAN-UP SET NO.
I.   EVAPORATION OF
                                  (ml) OF
     RINSE & BRUSHING OF NOZZLE, PROBE AND  GLASSWARE BEFORE
     FILTER.
          FINAL

          -BLANK ((

II.  FILTER CATCH
          SiC
          FINAL

. ((
(mg) - TARE
mg/ml) (
~/2s jS~ / ฃ ^ &
ml) =
fog)
mg)
                                        $ _ (Media Type & //)
                            /;t''"<-rs.'j — ?*-'-< ฃ>'•*" &. -^--^
                           (mg) - TARE   3 <~J. *ฃ _ (mg)
                                                                           ,*
III.  HYDROCARBON OBTAINED BY ETHER-CHLOROFORM  EXTRACTION ON
     WATER IN IMPINGER AND BUBBLERS.
                                                                                  mg.
                                                                                  mg.
IV.
FINAL
-BLANK (
PARTICULATE FROM
(mg) - TARE
mg)
EVAPORATION OF
IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION
FINAL (mg) - TARE
V.
-BLANK ((
_
PARTICULATE FROM
mg/ml) (
ml CONDENSED = ml)
(ml) OF
BUBBLERS, AND CONNECTORS AFTER FILTER:
FINAL (mg) - TARE
VI.
VFT
-BLANK ((
TOTAL PARTICULATE
BLANKS <ฃ<,/7 &/

ACETONE -
ETHER-CHLOROFORM
WATER =
/AP9 A
mg/ml) ( ml) =
= I + II + III + IV + V
mg/ ml =
mg.( FINAL
mg/ ml =

(mg)
- mg.
(ml) WATER
(mg)
ml initial
= mg) = mg.
RINSE OF IMPINGER,
(mg)
mg) = mg.
^fc.:/ /" mg.
FINAL mg .
mg/ml TARE mg.
mg - TARE mg)
mg/ml. FINAL mg .
TARE ;.iz .

                                           16,

-------
CLIENT
PORT LOCATION
DATE i
                                                        VALENTINE FISHER * TOMLINSON
                                                             Sf ATTLE, WASHINGTON

                                                           TRAVERSE SAMPLING DATA SHEET
                                                           IMPORTANT:  FILL IN ALL BLANKS
OPERATOR/S^J
RUN NQ.    ?. 7.
SAMPLE & METER BOX
Wffft BOX  AH	

FILTER NO..
                                                 O ^    C
                                                 87-5
                   /,
                                      . mg
     I
                                                                BAROMETRIC PRESSURE (PB).

                                                                LFJIK RATF  ;O /   CFM 0_

                                                                PORT PRESSURED VS)  C
                                                                PSN " PB * PS _-:
                                                                ASSUMED MOISTURE.
                                                                C FACTOR   ป9S

                                                                REF.AR.
                                                                       ."H20
                                                                                                                                      ':"'
                                                                             _"Hg
                                                                             _MKG
                                                                             _"Hg
                                                                                                                                                   oc
                                                                                                                             <"  t MAX VH.
                                                                                                                  '•>?<•'   7 '=-''" LK3"*    I 71?
                                                                                                              DTMFN5IONS
                                                                                                                                                 M
                                                                                                                                                F*
CLEAN-UP NO.'

BOX & PROBE  HEATER
                                                        SCHEMATIC OF TRAVERSE POINT  LAYOUT
                                                                                                         PROBE NOZZLE DIA. .K2 IN; AN- i^/j

                                                                                                         PROBE LENGTH  1 '  NUMBER   /? SIDE
  INSTANTANEOUS READINGS:   RECORDED 9 BEGINNING OF TIME INTERVAL
                                                                            AVERAGE VALUES. READ WITHIN THE TIME INTERVAL
  CLOCK
  TIME
 (24 MRS)
  //.'/fl
/ / y -7


             ELAP.
             TIME
             (MIN)
             JZ
             /•r
             '&
                      DRY GAS METER

                       (CUBIC  FEET)
                          _
                        3/-Z o
                                ,
                              ^/
                               -a
                         39.70
                           6 fc
DRY GAS TEMP.
INLET    OUTLET
                                       vo
                                         x
                                                 .7.7
                                                 Bo
BOX
TEMP.
                                                             Sir
                                                          •2-^X0
                                                          2.7V
                                                         ,2
IMPINGER
  TEMP.
  CF)
                                    POINT
PITOT VH
                                                                    S'2.
ORIFICE  AH
    ("H20)
                                                         DESIRED
                                                                                                   .^ -
                                                                                                  .i*/
                                                                                                  ,9$:
                                                                                                     ~7~
                                                 ACTUAL
 PUMP
 VACUUM
("Hg GA)
                                                                                                                    L> ?-
                                                                                                                      /'^'
                                                                                                                      S.,-0
                                                                                                                   ...Lt.^.
STACK
TEMP.
                                                                                                                               270
                                                                                                                               2*7.7.
                                                                                                                               290
                                                                                                                               2 S'O
OPACITY
  OR
 XC02
                                                                                                                                                  c- 3
                                                                                                                                                  -CJtJl.
 TOTAL
  •
                           . 30
 AVERAGE
                                                                                                                              277
                                                                                                               "He

-------
                             V \i.; rii lill-:,  I-' iSML,;  *, TUM.INSON
                      STAGK. f iH'.i I liKI-: CmM'liNT DATA MID CALi >  s.
                      / //C
Li" AYIuN

u '.' .. -UTO K

:,.V!!M.E Dux
                                                                    RUN NU.
                                                                    DATE
                                                                               No
                                                                                 .87-5
                                                         CuNTA iM-.K WliM.UTS  (^1:1
                     I Hi!  •- i
                                     i  WA'i'LH)
ii j ABSORBKD tV  SLLll'A Gi-L, mi
TUiAL 1100  LULL :.'.,: Li),  mJ
 VuL.  OF H.,0 V:-PM,<  ,d  70ฐ F.  AND I ATM.
 O.OA74 x  TOIAL hO
 MolSTURli  IN S'sACK GAS, %
 MLiLE FRjXOTioN ur  DRY GAS
 MOLECULAR wr. DC  S'IACK GAS
                                                                     INITIAL  i  ,NliT
                                                          .
                                                         3
%  MOISTURE  IN i.AGK  GAS •=
                               _^i  x  VOL.  11^0 vAL'ni<
                               VOL.  DRY GAS + VOL.  WcT GAS
MOLE FRAG'i 10,\ 
-------
                         VALENTINE, FISHER  & TOMLINSON
                LABORATORY ANALYSIS AND TOTAL  PARTICULATE SHEET
CLIENT
EVALUATION LOCATION  ^, / ฃ#

EVALUATION DATE      & - 2 <3
               DATE OF ANALYSIS

                         RUN NO.
                                               CLEAN-UP SET NO.
     EVAPORATION OF
(ml)  OF  A C
     RINSE & BRUSHING  OF NOZZLE,  PROBE AND GLASSWARE BEFORE
     FILTER.
          FINAL ~?(0bS'8.* (mg) - TARE  "? ฃ jo 2. O..Z.

          -BLANK ((ซCcfT7 ing/ml)  (  /ฃ"O   ml) =  .

II.  FILTER CATCH
                                                          (mg)

                                                           mg)
                                           . 7
                      	,  3 H   #	 (Media Type & #)
                      ,9                  36 ST. S"
          FINAL ซฃc?g,' 9   (mg)  - TARE   J5*5". 9	 (mg)
                                           , Q
 III. HYDROCARBON OBTAINED BY ETHER-CHLOROFORM EXTRACTION Ol
     WATER IN  IMPINGER AND BUBBLERS.
                                                                                  mg.
                                                                                  mg,
IV.
FINAL 6 7.2 6 2 .7
-BLANK ( />
(mg) - TARE (o ~) 2. 5~t> . /
5 mg)
PARTICULATE FROM EVAPORATION OF ;?<2_S 	 (ml)
IN IMPINGER AND BUBBLERS FOLLOWING EXTRACTION -
FINAL *? ~?/O 3. 9 (me) - TARE ~)~)d ff#.*l
V.
-BLANK (( ซ <2c/2ฃป
/^l ^ ml
PARTICULATE FROM /O
mg/ml) ( 2 .. */

ACETONE —
ETHER-CHLOROFORM =
WATER =
VFT/AP9 A
me/ml) ( /OO ml) = - ฃ>
4- II + III + IV + V
mg/ ml = rr
mg.( FINAL
mg/ ml =

(mg)
= /ฃ>. 8 mg.
WATER
(mg)
initial
• S~ tag) = /9,J~~ mg.
5E OF IMPINGER,
(mg)
mg) = -2 5s. 9 mg.
/?/,_? mg .
FINAL mg.
ig/ml TARE mg.
mg - TARE mg)
mg/ml. FINAL mg .
TARE rug .

                                             165

-------
                     VALENTINE,  FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
CLIENT
SAMPLING POINT LOCATION
                     RUN NO .
TIME OF SAMPLE COLLECTION
                                         HOW COLLECTED
                                         TIME OF ANALYSI
CUMULATIVE
% BY VOL. (DRY)
C02
C02 + 02
C02 + 02 + CO



ANALYSIS
#1
ANALYSIS
#2
/.
-------
CLIENT
                 /-/'/.v>V\
PORT LQCATI ON  /Aw/- K c xY<- • /1 //
DATE
        •/'T'AMBIENT
OPERATOR/S  / V d^ ' ^ r> /  ^ y- - W S. ••
RUN NO.	? :>  	RJ8-
SAMPLE & METER  BOX NUMBERS 4 t>(&   —s
      BOX AH
FILTER NO. 2L
CLEAN-UP NO. _
                                                         VALENTINE  FISHER * TOMLINSON
                                                               SEATTLE, WASHINGTON
                                                             TRAVERSE  SAMPLING DATA SHEET
                                                            IMPORTANT:  FILL IN ALL BLANKS
                                                                                        '/5-
BAROMETRIC PRESSURE (PB)jฃlLฃ
LEAK RATF  . -> .:   C.FM ffl    ^ S
PORT PRESSURE (Ps)  />    "H;0 -.
PcH - PB * PS   -• V. -I"'/	
                                                                                                                                                 HHg
                S
                      TARE  .^6- // '•>'
                                        mg
                                                                                                          rSN
                                                                                                          ASSUMED MOISTURE^
                                                                                                          C FACTOR !.&*>   _
                                                                                                          REF.AP.
                                                                                                                   '-(i.
                                                                                                                                                 "Hg
                                                                                                                                                 "Hg
                                                                                                                                  .X  MAX  VH.
                                                                                                                                                      OO
                                                                                                                                                      00
                                                                                                                                                       I
                                                                                                                                     .
                                                                                                                                   AREA  /.y J.J
                 .; BLANKS
BOX A PROBE HEATER SETTING
                                                          SCHEMATIC OF TRAVERSE POINT LAYOUT
STACK DIMENSIONSij^*l:
PROBE NOZZLE DIA. /4  IN; AN  • ;.ป/.3<-
PROBE LENGTH__JL_Nl!MBER_l?r SIDE_ป2
INSTANTANEOUS READINGS: RECORDED P BEGINNING OF TIME INTERVAL
CLOCK
TIME
(24 HRS)
/'Y : ^6

"^
TOTAL
AVERAGE
ELAP.
TIME
(MIN)
0
-•S
/ s
J'C
_-, 7 ..v -
> V
'/ 7-,
•> . >
/V. x'
DRY GAS METER
(CUBIC FEET)
*7C-.7B '^
") 7. q
^V-'/.^o
.<1:^' ฃV
/" * ' * '•if*
(_•* > / **-•
c •*> • ' ^
-^2. -/7,^
'•X '// /
DRY GAS TEMP.
INLET
. 76
CV '/
sv
'"//• ซ.' V
/C'-l
/rs
/ ^.H
,Z.ofa o
OUTLET
"/'•>
' 7 ?
r f ->
^ ->
*? z
76
77
/-T36,
tjC& ^>"$-(a
BOX
TEMP.
2.C50
1
.<*'.ซ
-2.70
2 -Jc.
•2C-C-
	
'y//
///,
IMPINGER
TEMP.
70
$-4 "'
	

///,
AVERAGE VALUES. READ WITHIN THE TIME INTERVAL
POINT
/ / 2
A I
.2...
3.
3
~<^l "
2
""-!..
tS'T"
	 >
	 f/.
•- —
2.0
////

PI TOT VH
(HH20)
2. /. S.../..J
.0 I
•PL/ 	
<_ฃ/<:•
i^rr"
/ PAS
	 -o/
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                         VALENTINE,  FISHER & TOMLINSON
                LABORATORY ANALYSIS  AND TOTAL PARTICULATE SHEET
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BLANKS ฃ
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                     VALENTINE, FISHER & TOMLINSON
                   ORSAT DATA AND CALCULATION SHEET
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TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
1.
4.
7.
9.
12
15
16
17
a.
=lฃ = CRT NO.
2.
7:TL = AND SUBTITLE
Source Sampling Residential Fireplaces For
Emission Factor Development
AUTHOR(S)
W.D. Snowden, D.A. Alguard
W.E. Stolberg
, G.A. Swanson,
PERFORMING ORGANIZATION NAME AND ADDRESS
Valentine, Fisher & Tomlinson
520 Lloyd Building
Seattle, Washington 98101
. SPONSORING AGENCY NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning & Standards
Monitoring & Data Analysis Division
Research Triangle Park, N.C. 27711
. SUPPLEMENTARY NOTES

3. RECIPIENT'S ACCESSIONปNO.
5. REPORT DATE
November 1975
6. PERFORMING ORGANIZATION CODE
8. PERFORMING ORGANIZATION REPORT NO.
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
68-02-1992
13. TYPE OF REPORT AND PERIOD COVERED
Final July-August 1975
14. SPONSORING AGENCY CODE

. ABSTRACT
One typical residential fireplace was source sampled for particulate (both
filterable and condensible) , polycyclic organic materials (POM), volatile hydro-
carbons, and carbon monoxide emissions. Testing was conducted using alder,
Douglas Fir, Locust, pine, and coal. Particulate was sampled and analyzed utiliz-
ing EPA Method 5. POM was collected on a TENAX adsorbent and analyzed by GC-MS
methods. A rough energy balance on wood combustion in fireplaces was performed.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS

TEN AX
Emissions
Parti culates
POM
Fireplace
19. DISTRIBUTION STATEMENT
Release Unlimited
b.lDENTIFIERS/OPEN ENDED TERMS C. COSATI Field/Group

19. SECURITY CLASS (This Report) 21 . NO. OF PAGES
Unclassified 173
2O. SECURITY CLASS (This page) 22. PRICE
Unclassified
EPA Form 222O-1 (9-73)

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