EMISSION TESTING OF CALCINER OFF-GASES
AT FMC ELEMENTAL PHOSPHORUS PLANT
POCATELLO, IDAHO
EMISSION TEST FINAL REPORT
VOLUME II
APPENDICES
August 1984
-------
DCN #84-231-060-56-04
EMISSION TESTING OF CALCINER OFF-GASES
AT FMC ELEMENTAL PHOSPHORUS PLANT
POCATELLO, IDAHO
EMISSION TEST FINAL REPORT
VOLUME II
APPENDICES
August 1984
Contract No. 68-02-3174
Work Assignment No. 131
EPA Project Officer:
S.T. Windham
Contractor:
Radian Corporation
Post Office Box 13000, Progress Center
Research Triangle Park, North Carolina 27709
Prepared By:
R. Jongleux, A. Blackard, J. McReynolds, and C. Stackhouse
Prepared For:
U.S. Environmental Protection Agency
Office of Radiation Programs
Eastern Environmental Radiation Facility
Montgomery, Alabama 36193
-------
DISCLAIMER
This report has been reviewed by the Office of Radiation Programs,
U.S. Environmental Protection Agency, and approved for publication.
Approval does not signify that the contents necessarily reflect the
views and policies of the U.S. Environmental Protection Agency, nor does
mention of trade names or commercial products constitute endorsement or
recommendation for use.
ii
-------
TABLE OF CONTENTS
APPENDIX A Calculations and Complete Data A-l
APPENDIX A-l Complete Particulate Matter Results A-2
APPENDIX A-2 Particulate Matter Calculations and Andersen
Cascade Impactor Calculations A-114
APPENDIX A-3 PADRE Entry Forms - Run Data and Filter Weights . . A-135
APPENDIX A-4 PADRE Computer Printouts A-150
APPENDIX B Field Data Sheets B-l
APPENDIX B-l Traverse Point Locations B-2
APPENDIX B-2 Preliminary Measurements B-12
APPENDIX B-3 EPA Method 5 - Stack Field Data Sheet B-36
APPENDIX B-4 EPA Method 5 - Sample Train Recovery Sheet .... B-71
APPENDIX B-5 SASS Field Data Sheets B-91
APPENDIX B-6 Andersen Particle Sizing Field Data Sheet B-95
APPENDIX B-7 Process Sample Data Sheets B-116
APPENDIX C Sampling and Analytical Procedures C-l
APPENDIX C-l Detailed SASS Operating Procedures (ORP
Program Modification) #2 C-2
APPENDIX C-2 General Procedures for Operation of Inertia!
Cascade Impactors C-12
APPENDIX C-3 Radiochemical Determinations of Lead-210 and
Polonium-210 in Dry Inrganic and Biological
Samples by ORP/EERF C-20
APPENDIX D Field Analytical Results D-l
APPENDIX D-l SASS and EPA Method 5 Field Gravimetric Results . . D-2
APPENDIX D-2 Field Gravimetric Logbook D-6
APPENDIX D-3 Alternative EPA Method 3 Results
GC/TCD and Chromatograms D-25
(continued)
iii
-------
TABLE OF CONTENTS
Page
APPENDIX E Participants and Field Log E-l
APPENDIX F Meter Box Calibrations F-l
APPENDIX G Additional Plant Information G-l
APPENDIX G-l FMC - Replicate Particle Size Measurements
and Calculations ' G-2
iv
-------
APPENDIX A
CALCULATIONS AND COMPLETE DATA
-------
APPENDIX A-l
COMPLETE PARTICULATE MATTER RESULTS
-------
so i-.i iF<
METHOOS S
x r-i r T x o r*4 o F^
•£> r
: F< u-i s
PARAMETER
DEFINITION
T t (m i n . 1
Dn (in. )
Ps(in.H2Q)
VIM (CU. ft. )
Vw(gm.i
Pm (in. H2O.)
Tm>F>
Pb(i n.Hg. t
•/, cor
•'. 02
7. N2
SQRTDELPS)
As(sq.in.)
Ts(Fi
Vm ( dsc-f >
Vw gas ( sc-f )
"'. iTioi sti ire
Md
MWd
'J=, i t pm)
Fl ow ( ac-f m )
Fl OM ( ~CITHTI)
Flc
v. I
•, ErA
DGM
Pq
Cp
dH
dP
TOTAL SAMPLING TIME f
SriMPLING NOZZLE DIAMETER
ABSOLUTE STACK STATIC GAS PRESSURE
ABSOLUTE VOLUME OF GAS SAMPLE MEASURED BV OGM
TOTAL STACK MOISTURE COLLECTED
AVERAGE STATIC PRESSURE OF DGM
AVERAGE TEMPERATURE OF DGM
BAROMETRIC PRESSURE
CARBON DIOXIDE CONTENT OF STACK GAS
OXYGEN CONTENT OF STACK GAS
NITROGEN CONTENT OF STACK GAS
AVE. 3D. ROOT OF S-PITOT' DIFF. PRESSURE-TEMP. PRODUCTS
CROSS-SECTIONAL AREA OF STACK', DUCT)
TEMPERATURE OF STACK
STANDARD VOLUME OF GAS SAMPLED ,Vm(std)
STANDARD VOLUME OF GAS SAMPLED,Vm(std).^i
VOLUME OF WATER VAPOR IN GAS SAMPLE,STD
WATER VAPOR COMPOSITION OF STACK GAS
PROPORTION, BY VOLUME,OF DRY GAS IN GAS
MOLECULAR WEIGHT OF STACK GAS,DRY BASIS
MOLECULAR WEIGHT OF STACK GAS,WET BASIC
AVERAGE STACK GAS VELOCITY
FLOW RATE (ACTUAL STAC'.. COND.)
FLOW RATE(ACTUAL STAC! CPND.i
,AS DRY STD. CF
DRv SVD. i-M
SAMPLE
LB/LB-MULE
LB/LB-MOLE
AVERAGE
AVERAGE
AVERAGE
AVERAGE
PERCENT
PERCENT
DRY GAS
DRY GAS
STACK
PI TOT
STACK
STACK.
STACK
STACK.
GAS
GAS
GAS
'"-'AS
VOLUMETRIC
VOLUMETRIC
FLOW
FLOW
RATE ( OR i'
PATE(DRY
BASIS)
ISOK INET 1C
EXCESS AIR IN STACK GAS-
METER
METER CORRECTION FACTOR
STATIC GAS PRESSURE
COEFFICIENT
ORIFICE PLATE DIFF. PRESS.
PI TOT DIFF. PRESS. VALLIE
VALUE
*** EPA
STANDARD
CONDITIONS
Temperature = 63 deg-F (528 deg-R>
Pressure = 29.92 in. Hg.
A-2
-------
:<=*D i *=%INI
=* MI E: ~r H o o
PLANT
PI.ANT SITE
SAMPLING LOCATION
TEST $
DATE
TEST PERIOD
FMC
POCATELLG
INLET 2-2
A-l
1O/27/S3
1505-1810
I DAHG
PARAMETER
VALUE
Sampling time 99.247
Absolute stack pressure(in Hq' 25.16O74
Average stack temperature
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST «
DATE
TEST PERIOD
I *=»IM S O *_J R C3 IE€ TEST
M EE: T" n o o s s — is
._ F< «=: s u L- T s
FMC
POCATELLQ , IDAHO
INLET 2-2
A-l
15O5-1810
PARAMETER
RESULT
Vm(d=ct)
'-'m (dscm)
'•Jw gas (sc-f >
'J^ gas (scm)
v. moist1.1re
Md
56. 4T<"O2
MW
v.'s <-f pm)
Fl ow '. aci HI '
F] CfW ( acrnin)
Fl ow (dsc f m)
Fi ow » dsc mm)
'•'. I
•: EA
4. 6^7C?4>:'7
. 1325233
7 . 653925
. 92346O8
29.872
28. 96333
5202.917
1586.255
17
-------
OL.HRCE:
^ METHOD S
c LJ L_ «^ T E: i_ o #^ D j M r3
FMC
POCATELLO , IDAHO
INLET 2-2
A-l
PLANT
PI..MNT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
1505-1810
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams. dsc-f
Gr ems / ac-f
Gr ei ns/dsc-f
Grai ns/ac-f
GraiTis/dscm
Gr a.iTi= •' a. cm
Founcls/dsc-f
Pounds/acf
Founds -'Hr
t i 1 oqra.ms .'Hr
5.445910O
O. 0^645"/8
O.O3^2O50
1.4883430
O.&O49338
3.4O59230
1.38433OO
(j. i") >')("> 21:2"?
O.OOOO364
932.O694OOO
422.78390OO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
("I. OOOOOOO
* BACK-HALF IMFINGER ANALYSIS WAS NOT REQUIRED
Program Ke'-^i si on : 1 /
A-5
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
INLET 2-2
10/28/83
0958-1234
PARAMETER
VALUE
Sampling time (min.) 144
Barometric Pressure (in.Hq) 25.68
Sampling nosnle diameter (in.) .247
Meter '-'olume (CM.-ft.) 129.9O8
Meter Pressure (in.H2Q) 2.4^
Meter Temperature (F) 1O5.56
Stack dimension 4ir?73.5
Stack Static Pressure
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
ME: THODS
F* EE: s u i_ T
FMC
POCATELLQ
INLET 2-2
A-2
1O/23/83
0958-1234
IDAHG
PARAMETER-
RESULT
Vffl
-------
F;:#=*D i
E: R- #=% rt E
=t T T. O LJ L_
PLANT
PLANT SITE
SAMPLING L OCATION
TEST #
DATE
TEST PERIOD
TEES^T
J-HTJD S
i_o<^»o i r-JiG
FhC
POCATELLO , IDAHO
INLET 2-2
A-2
1O/28/83
O958-1234
PARAMETER
FRONT-HALF
TRAIN TOTAL.
Total Grams
Grams ''dsc-f
Grams/ ac-f
Grai ns -'dscf
Gr ai n«''ac: f
Grams/ dscm
Founds /d=c f
Pounds /act
Pounds/ Hr
K i 1 oq r aiTis / Hr
O. 0
O. "77ijil)56iT1
O.3317126
1.7621980
O.759O9O9
O. <"iOO 1 1OO
O.OOOO474
525.O54&OOO
233.1632OOO
O. U(.)OO<.)<
O. OOOC>OO.O
O. OOC'OOOO
0.OOOOOOO
O.OOOOOOO
'•"'. OOOOOOO
O. OOOOO''>O
O.OOOOOOO
O . OOOt x")OO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revision:]
A-8
-------
El F=-
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
I ^ivl SOLJFtOEZ TEST
Ml El T~ 8HI O D S — S
FMC
POCATELLO , IDAHO
INLET 2-2
A-3
1O/23/83
1453-1302
PAPAMETEF
VALUE
Sampling time (min.)
E'arometric Pressure (i n . Hq )
Sampling nozzle diameter (in.)
Meter Volume
Average stack temperature
• .^--H /
131.222
2. 68
116.27
4973.5
3,15
293.614
25.O8O74
573.O8
9.67
1 4. 96
75.37
35.2989
1.OO38
.84
A-9
-------
F^ I tv|^l_
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
METHODS S—:
RE
.TS
FHC
POCATELLO
INLET 2-2
A—o
1 O/ 2S .''83
1453-1302
IDAHO
PARAMETER'
RESULT
Vm'dscf)
V\T\ < dscm)
Vw q*s < sc-f ^
^'"^ gas (scm)
"/. moi sture
Mel
MWd
MW
'•-' s < -f p m)
'•j's (mpm)
Fl ow (acftri)
Flow(acmm)
Flow «,dscf m)
Flow(dscmm)
V. I
'/. EA
104.37^5
1.956027
13.843^
.392O593
11.7O995
.3829005
30. 145
-------
Ft *=» O X <=* rvl SO I.. J R C EZ "TEST
=> METHOD S
F-#=%R:~r i ci_ii._
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
LO^D I Mt3
FMC
POCATELLO , IDAHO
INLET 2-2
A-3
1O/2S/83
1453-1802
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams .'ac F
Grai ns-'dsc-f
Grai ns -'a.c-f
8ram= /dscm
Grams/acm
Pounds/dsc-f
Pounds/ac-f
Pounds/Hr
Ki1oqramn/Hr
31 . 9679OOO
O.
O.
4.
3O62662
1158482
72568~0
1 . 7875380
1O.S1426OO
4 . O9O6O 1 0
O . OOO&753
O . OOO2554
29i:T'T>. 4>33OOOO
1 36O . 624OOOO
O.OOOOOOO
0. OOOOCiOO
0.OOOOOOO
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revi si on : 1 / 1
-------
Ft #=* D I *=* !M S OILJ Ft C- E
=* r-n EE: ~r H o r> 2: —
PMC
POCATELLO
INLET 2-2
A-4
1O/31 ''83
O942-1359
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
IDAHO
PARAMETER
VALUE
Sampling time
-------
r D T #^ |v| S CM J Ft O EH!
«=* r* SEE: T HODS s
IF" .1 IM ^t L. Ft E S LJ l._ T S
PL--, I'IT
PI MJJT SITE
S A M P L. I N G L O C A T I O N
IF 91 #
DA TE
TEST PERIOD
FMC
POCATELl Q
INLET 2-2
A-4
1O/31,03
Q942-1359
"T ETJ. S
I DAt ID
PARAMETER
RESULT
Wm (dsc-f /
'-'iT, ( d5C,7l >
Vw gss
Fl ow (aciTifii)
Fl ow (else: f,Ti)
Fl ow (elsemm)
"/. I
So.92357
2.461676
10. 6<"i248
.30O2622
10.87143
. 8v 1 235-7
29.854
2S.5053
496G.O42
1512.203
171310.9
4851.524
67826.56
1920.848
92.42914
486.5139
Program Revi 3\on: 1
A-13
-------
D I
£3 O l_J F< O El
PLANT
PLANT' SITE
SAMPLING LOCATION
TEST 4*
DATE
TEST PERIOD
FMC
PGCATELLO
INLET :;-2
A-4
l'')/31/37
0942-135*?
El £3 T
I DAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dscf
Grams •'sci
Orai ns/dsc f
Grai ns • s.c f
Grains/ d = ciTi
Gram=. a cm
Pounds.dsc f
Pounds /sc. f
Pounds-'Hr
Kiloqram=/Hr
19.31^
O.2222343
3.429O76O
1.357663O
3.106S75O
O. OOO490O
0.OOO194O
O. OOOOO'">O
O.OOOOOOO
<"'. OOOOOOO
O.OOOOOOO
O.OOOOOOO
O. OOOOOO<"»
O. OOOO< 'OO
O.
'). oOOOOOt'i
• . L>'
C?O4. 567400O
* BACK-HALF IhPIMGER ANALYSIS WAS NOT REQUIRED
Program Re --i si on : 1 / 1 6 / B4
A-14
-------
F< ^ o
ip» r-4
so i..j FV- c ei
H O O S: —
PLANT
PLAN! SITE
S A M P L I N C3 L H C A T IG M
TEST tt
DATE
TEST PERIOD
FMC
POCATEI. LD
INLET 2-2
A--SASS-1
-a -
IDAHO
(TOTAL FRONT HALF''
10/
:7-'83
i- 1 3O<".>
PARAMETER
VALUE
Sampling time .495
Meter Volume (cu.-ft.) -- dimension ( sq . i n . ^ 4973.5
•Stack Static Pressure -8.15
Stack Moisture Collected (grn.) 1475.65
Absolute stack pressure(in Hq) 25.16O74
Average stack temperature (F) 482,9
Percent CG2 7.6
Percent: O2 16,4
Percent N2 76
Delps Subroutine result 42.6836
DGM Factor -98
Pi tot. Constant .34
A-15
-------
r> x #=» ir-4 s o LJ Ft c IE: T
e: F> *=* M EZ T m o r> s s —
!=• T Ixl i^ L_ Ft EE S U l_ T S
PLANT
F'LAMT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATEL.LO , IDAHO
INLET 2-2
A-SASS-1 (TOTAL FRONT HALF')
30/27/83
0735—13OO
PARAMETER
RESULT
Vm
Vw gas (scm)
7. moi sture
Md
MWd
MW
Vs <-f pm)
'-'s (.mpm)
Fl ow (>acf m^
Fl ow < acmm)
Flow(dscfm)
Fl om t'dscmm)
V. I
V. EA
797.3911
22.58212
69.5769
1.97O41S
3.025313
.9197469
29.872
28.91924
.b817.92
2078. <^34
235478.7
66t>8. 755
101988.2
2388.3Oo
83.39221
447.5933
Program Revi si on : 1/3
A-16
-------
F< i
f='f=-£* r-1EE
< 1"" I. O i. J l.._ *P» "!
PLANT
PLANT SITE
SAMPL I Ni.3 LOCAT I ON
TEST *t
DATE
TEST PERIOD
£3 CM. j IRC: IE: ~r
noo s
r EEI i— O ^ t>
FhC
POCATELLD
INLfc'T 2--2
M-SASS-1
10.27/83
O735--13».'O
1. PAhG
'-.TOTHL FSCJNT HALF)
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams / ac-t-
Grai ns /dsc-f
Grai ns -' act
Poijnds/dsc f
Pounds / ac: f
FoL-nds/Hr
H: i 1 oqr-am= /'Hr
. O 1. 3 '2 CO O
. 074OO 73
141^410
4V45RA2
J.6132J.70
1.131311 O
O . OOO 1 632
452. 9
O.OuOOOOO
0. OOOOOO(')
0. '"iOO<".'C)OO
O.OOOOOOO
'"'. OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Re-^i si on : 1 • 1
A-17
-------
PLANT
PLANT SITE
S^MFl ING L-OCATION
TEST tt
DATE
TEST PERIOD
PMC
PDCATELLO , IDAHO
INLET 2-2
A-SMSS-! (FILTER/ 1 MICRON;
3o •- 1 3OO
PARAMETER '-'ALUE
Sampling time (min.)
Barometric Pressure (in.Hq) 25.76
Sampling norzle diameter (in.) . 4l!?5
Meter '-'Glume 1.58
Meter Temperature (F> '3 i . ^
Stack dimension >, sq . i n . > 4^73.5
Stack Static Pressure 25.16O74
Average stack temperatt.tre
-------
FC £* D I tP* UNJI S O H. J F<
> *=* M El ~T Ml C1 D S
I Ixj «£* I ._ F< E S LJ l_
T E
PLAMT
Fl.r-NT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FHC
POCATELLO , IDAHO
INLET 2-2
A-SASS-1 (FILTER/I
1O/27/S3
O735-130O
MICRON)
PARAMETER
RESULT
Vm(dsc-f )
VlTl (dSCffi)
Vw gas < sc-f >
VIM gas (.sc
"'. moisture
lid
MW
'•.'5 <;
'-'s
-------
FC i^ D T
IM S O !_J Ft O
T IE S3 T
E: IF> ^> r-a E
i c: I_JL_
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FhC
PGCATELLG , IDAHO
INLET 2-2
A-SASS-1 (FILTER/I MICRON)
10/2~V83
O735-13OO
PARAMETER
Filter
1 Micron
Total Grams
Grams/dsc f
Grams -•' acf
Grai ns < dsc-f
Grai ns/ ac-f
Grams/dscm
Grams /'acm
Pounds' dsc-f
Pounds /ac-f
Po' ind= /Hr
I', i I oqrams/Hr
O. 3351 40<->
O . OOO1820
O. OO64852
(j . (!'028O88
O. 00^4276
80
O.47^1300
O. OOOfcOOc?
O. OOO4(.il6O
O.021219O
(). 0'.''-' 1 ^ O 2
O.OOOOO13
O.OOOOOO6
8.1O8434O
3. 677961.0
Pr oqr a.iTi Re-/ i si on : 1 / 1 6
A-20
-------
SCM-IRrOEJ.
1 1-8 O O J2 —
C FXif^lAj I
PLANT
PLANT SITE
SAMPLING LQCA1 ION
TEST tt
DATE
TEST PERIOD
"I"ET.
FMC
POCATELLO , IDAHO
INLET 2-2
A-SASS-1 <3 MICPON/1O MICRON H- PROBE)
1O/27/83
O735—13OO
PARAMETER
VALUE
Samp1i nq t i me (mi n. )
Barometric Pressure (in.Hq)
Sampling nozzle diameter (in. >
Meter Volume (cu.ft.)
Meter Pressure (in.H2CP
Meter TeiTiper ature < F t
Stack dimension
-------
;; f*D r #=»r-4 soi..iF< c E:
=> MI E ~r n o o s 2: —
PLAN r
PLANT SITE
SAMFl ING LOCATION
TEST *
D^TE
TEST PERIOD
FMC
POCATELLO , IDAHO
INLET 2-2
A-SASS-3 (3 MICRON/I" MICRON + PROBE)
10.'1:7/83
0 735— 1 3' " '
PARAMETER
RESULT
Vm
'v'm (dscm >
'-^'w gas < =cf ')
Vw gas ' scm)
''. moi stur e
Md
MWd
MW
^ = < + p m )
F] ow (ac-f m)
Fl ow (wcmm)
Fl ow ( dsc-f m )
Fl ow ', dscniiTi ')
••'. I
:'. EA
7Q7.3911
22.58212
3.0257]-?
21. 872
23.91.924
6817. 92
2<">73. 634
• '• T e- /i -7 r-> ~^
j^-1 wJ 4 r O • /
6668. 755
1O1938. Z
2888. 3O6
83. 39221
447.f,983
Prog ream Revi si. on : 1 / 16/34
A-22
-------
F< ^ O T £•* !"-4 J3 C3 ?.J Fv" O El "T" El:
E: iF> *=* r^iEfTHOD S
F=- ipfc R: T- i: c; LJ L_ ^ T E: i_ o ^ o i
FMC
PLt-iNT SITE
i< r-i M P L IN G L O C A T I O N
TE'ST #
DP.TE
TEST PERIOD
PGCATELI.O , IDAHO
I NL.ET 2 - 2
A-SASS-1 (3 MICRON/1C MICRON +•
PARAMETER
3 Micron
10 Micron S-Probe
Total Srsms
Grarris /dsc f
Grams., acf
Gr ai n= /'dscf
Gr ai n= .'acf
Gr r?m= /d = cm
Grams/3cm
Pounds .'dscf
Poi md = / :?.c t
Pounds/Hr
KiIoqrams/Hr
3.13 7O5OO
O.CO39341
O.OO17O39
0. 06O ••'O33
O.O262vl4
O. 1339146
O.OoO1653
0. O'.""JOOS7
(.'. OOOOO38
53.O8353OO
J4.O7353OO
55.U619OOO
0.0690526
O.O299O74
1.0654310
O.46147O7
2.433246O
1 . O5o(.'29O
0 . ' "!>'"> 1 523
O „ OO659
931.7233OOO
422.6294OOO
Program Revisi on: 1/16•
A-23
-------
V^JO I ^r-J 300 ROE-. TE". ST
r-i E: ~r 1-1 o D s — s
D «=k T *=;» >
PLANT FMC
PLANT SITE POCATELLO . IDAHO
SAMPLING LOCATION INLET 2-1
TEST # B-l
DATE 1O/27/83
TEST PERIOD 14O1-1753
PARAMETER
VALUE
Semplinq time
Barometric Pressure (in.Hq>
Sampling nozzle diameter '.in.)
Meter Volume (cu.ft.)
Meter Pressure (in.HZO)
Meter Temperature iF)
Stack dimension (sq.in.)
Stacl- Static Pressure '. in.H2D>
Stack Moisture Collected (gm)
Absolute stack: pressure', in Hq)
Average stack temperature (F)
Percent CO2
Percent O2
Percent Nlv
De 1 p 5 Subr ou 11. ne r esu 11
DGM Factor
P i t ot Con stan t
144
25. 7&
.25
110.176
1 .64
10O.B
4^73.5
-8
83.38301
25.17177
567.. 16
S. 55
1 5. 84
75.61
25.3988
A-24
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST aft
DATE
TEST PERIOD
SOLJFv
T H O D S S3 -
Ft El S31_J l_. T S
FMC
POCATELLQ
INLET 2-1
B-l
10/2^/83
1401-1^53
IE: T HE: s nr
IDAHO
PARAMETER
RESULT
Vm (dscm)
Vw qss < sc-f >
Vw qas (Ecrn
V. moisture
Md
V 5 < -f p (Ti )
Fl ow (5.c-f m)
Fl ow (acfftm)
F.I ow (dsc-f rn '
Fl ow ('dec mm)
v. I
V. EA
3^.63776
2.538541
3.931509
,1113403
4.20171
.^579329
3O. OOlt>
29.49733
4095,223
1248.544
141441.6
4OO5.626
53598.O1
1659.496
107.fc.945
j.84. 3o
-------
F<#=*
F-rf^FtT T
PLANT
PL-AiJT SITE
SAMPLING LOGAT ION
TEST #
TEST PERIOD
EsouFtoEi TIE:::
-•» o o s
"TC: l-O^D T.
FMG
POCATELLO , 1
INLET 2-1
B-l
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dect
Grams/a, c-f
Grai n= .'dscf
Gra 3 ns/ac-f
Grams/d=cm
Grams/acm
Pounds'dsc+
F'oiinds .'ac-f
Pounds /Hr
l-'i ] ogrfiiTi=/Hr
0. 44 O9 10O
i.i. OO-t^ 188
O . OOI!'.>3~78
O . O"' 58^70
O. 0314435
t:>. 1736828
O . OOOO045
38 . 1 33<">oOO
1 7 . 2 i:? 7 04 CO
# BACK-HALF IMPIIMGEP ANAL~T SIS WAS NOT REQUIRED
P r o q r a m K e -J i 5 i o n : 1 / 1 o / 8 4
A-26
-------
EE: TIEE:ST
:$=•£* t-1 E r H O O S — '5
FC*=%UJ o^~r*^>
FMC
POCATELLO , IDAHO
INLET 2-1
B-2
10/28/83
1027-1308
PLANT'
PLANT SITE
SAMPLING LOCATION
TEST tt
DATE
TEST PEP I (3D
PARAMETER VALUE
Sampling time (min.) 144
Barometric Pressure 85.47
Stack dimension 159.955
Absolute stack pressure'in Hq) 25.O9177
Average si-ack temperature (F) 5O3.54
Percent CC2 7-15
Percent O2 16.69
Percent N2 76. 1-bOOl
Delps Subroutine result 25.6975
DGM Factor -999
Pi tot Constant .34
A-27
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
M El T l-l O D S
._ FcEISUJL.
PMC
POCA1ELLO
INLET 2-1
B-2
10/28/S3
1O27-13O8
IDAHO
PARAMETER
RESULT
VIT, idsc-n
Vm (dscm>
Vw qas < sc-f )
'•'. moisture
lid
MWd
MW
V 5 < -f p in i
Vs ', mpm;
Fl ow '. actm >
Fl o*»J < acmiTi)
Fl ow (dsc-f rn)
Fl o
': EA
2.62349V
7.5418^9
.21 358t.
7.528362
.^247164
2V.31 lo
28. 92230?
4 1 1 0 . 117
1253. OS4
4O20. 194
6O324 . QZ
17O8. 399
103. 1 127
488.5485
Prog r siu Re vision: 1./ 1 o -' y 4
A-28
-------
Fc#=nr> n: ^i-xi SOURCE
EF i=-<=* METHOD s
r=- ,ft r-- ir T o Lj i_ <^ T
PI At'JT
PLANT SITE
SAI'IPL. ING I .OCA T I ON
TEST #
DATE
TEST PERIOD
I...
FMC
POCATELLO
INLET j-i
B-2
tO/28/33
1027-1308
T f-J£3
I DAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
l Grams
Grairis/dscf
Graffls/?c f
Grai ns' dsc-f
Grain=/scf
Gr aiTl5/d = -|Tl
Grams/scm
Po< ind= ''dsc-F
Pounds / i-c f
Pounds/Hr
Ki 1 ogram=/Hr
1.564O4OO
O.O168834
O.O071747
O.26O5111
O. 1 1C) 7 053
0.5961533
O.253338O
O.OOO0372
O.'-OOO158
134.7461OOO
61.12O42OO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOu
0.OOOOOOO
O.OuOOOOO
O.OOOOOOO
# BMCK-HALF IMPIMGER ANALYSIS WAS NOT REQUIRED
Program Rev 3 si on: I
A-29
-------
PL At I P
PLANT SITE
SAMPL ING LGCAT I ON
TEST #
DATE
TEST PEP I GO
JT ^iTvl £3 O fl. J FV LIT t=.
S-JETMiOD S —!
>
FMC
POCAI'ELLO
INLET 2-1
B--3
10/23/33
1453-1734
I DAHO
PARAMETER
VALUE
bamp ling t i me (rn in.)
Barometric Pressure (in.Hq)
Sampling nozzle diameter (in.)
Meter Volume (cu.-ft.)
Meter Pressure
Meter Temperature (F)
St.act; dimension < sq . i n . >
Stack Static Pressure (in.HZ'G)
Stack Moisture Collected '.qmi
Absolute stack pressure'in Hq)
Average stack temperature 'F)
Percent CO2
Percent (12
Percent N2
Delps Subroutine result
DGM Factor
P i t at Con 51 an t
144
25.68
1O3.1:?23
1.62
i O 1 . 1 4
4973.5
-S
224.731
25.O
1 4. 64
75. O6
25.67^5
A-30
-------
R^OIn^rvj SOURCE TEST
E F=-
-------
Ft *=* O I ^ tv8 SO L
E: IF- *=* M IE: T n o o s
"I 1^ S T
¥=• £=» Fv- T
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
L-_ O f* E>
FMC
POCATELLO
INLET 2-1
8-3
1453-1734
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/ clsc-f
Grams /ac-f
Grsi ns/dsc-f
Grai n5-'ac-f
Gr am= / clscm
Gr'ams/ acffi
Pounds'dsct
Pounds/ac f
Pounds -'Hr
Ki 1 oqr ams -'Hr
.413^300
.O2S7171
. o 1 OS 1 52
.4431O45
.1668735
.014OOOO
.3818346
.OOO0633
.OOOu 238
.1.71 4OOO
"2. 157r-?4OO
'"i. OOOOOOO
O.OOOOOOO
O.OOOOOOO
O. OOO<"'OOO
0.OOOOOOO
O.OOOOOOO
0. OOOOO'X)
0. i~>OOOOOO
'."i. OOOOOOO
# 8ACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Rev j si on: 1
A-32
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST 4+
DATE
TEST PEPIOD
I rf^r-S £3 O U Fc C::
r*iE:~rnoE> s
FMC
POCATELLO
INLET 2-1
B-4
1O/31 /S3
0^47- 1253
1 DAHO
PARAMETER
VALUE
Sampling time (min.)
E-'arometri c Pressure < i n . Hq '
Sampling nozzle diameter < i n . >
Met er Vol ume ( cu .ft.)
Meter Pressttre
Stack dimension < sq . i n . )
Stack Static Pressure (in.H2O)
Stack Moisture Collected
-------
SOURCE TEST
METHODS S —Si
f— X r
PLANT FMC
PLANT SITE POCATELLO , IDAHO
SAMPLING LOCATION INLET 2-1
TEST # B-4
DATE 10/31/33
TEST PERIOD 0^47-1253
PARAMETER
RESUI. I
Vm (dscm '
Vw gas '', sc-f '
Vw qas
-------
Ft *=* D T «=* INI £5 O I_J Ft
- »=*
T C
PLANT
PLANT SITE
SAMPLING LOCATION
TEST *
DATE
TESF PERIOD
l_O*=iD
FMC
POCATELLO
INLET 2-1
B-4
10/31/33
O947-1253
TEST
E INIC3
, IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams•dsct
Grams/a.c-F
Srai ns/'dsc f
Grai ns/acf
Grams <' dscm
LT r a i~n = / a. c m
Pounds.dsc+
Pounds/acf
Founds/Hr
h i 1 oqr « m 5 '' Hr
3.7135500
O.0427612
0 . 01 6663-0
O.6598051
0.2571098
1.5O9898O
O.588369B
O.OOOO943
0.OOO0367
3 1 3 .
-------
""*• i— ~r~
-j- 1ZZ. i
PLANT
PLANT SITE
SAMPL I NG I..OCAT I ON
TEST #
DATE
TEST PERIOD
FMC
PUC'MTELL.D
OUTLET 2-
C-l
li')/Z6.'R3
- t 057
IDAHO
PARAMETER
VALUE
Samp ling t: i me (m i n . )
Barometric Pressure (in.Hq >
Sampling nozzle diameter (in.)
Meter Volume (cu.t-t.i
Meter Pressure (in.H20)
Meter Temperature (F>
Stac^: dimension \sq.in. '
Stscl-: Static Press'.tre
Stack Moist LI re Collected (qm'i
Absolute- st.sc!- pressure* in Hq >
A'^-ersqe stack- temperature (>F)
Percent CG2
Percent 02
Percent N2
Del ps Subroutin<= result
DGM Factor
Pi tot Constant
96
-.c- -re-
. 194
54.428
. 7?Q
44.f'5
4^0.634
.4J
L 7^. 2r>3
I"3. 7SO88
1 41 .^38
5.44
17.7
7fc.S6
22™ 4484
. '?
-------
EE: F=-
PL.ANT
PLANT SITE
S A M P L IN G L O C A T IQ N
TEST tt
DATE
TEST PERIOD
FMC
POCATELLD
OUTLET 2-:
C-l.
1O/26/83
OS39-1O57
I SIT
IDAHO
PARAMETER
RESULT
Vm (dscm )
'^w gas ( sc-f )
\j\rt gas < scm i
v. moi sture1
Md
hWci
MW
Fl ow < ac-
Fl ow (^a
Fl ow ( d=cf m)
Fl OW
"•'. I
'.'. EA
49.08194
1.390OO1
8.355122
.2366171
14.54657
.8545343
29.5784
27.89414
360o.831
1O99.644
119993.1
3398.2O5
775OO.45
2194.813
118.9239
-------
R:#=»D i
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
METHOD S
T E 1— O £* D I 1T-J G
FMC
POCATELLO , IDAHO
OUTLET 2-2
C-l
1O/26/33
0839-1O57
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dscf
Grams/ ac-f
Grai ns/dsc-f
Gr sins/ac f
Grams ''dscm
Grams -' acm
Pounds •' dsct
Pounds /ac:f
Pounds -'Mr
Ki1oqrams/Hr
O.15767OO
O, O'.>32 124
O.0020743
O.O495671
O.O32O141
0.11742^3
. 077::61 o
OOOOO7 i
. OOO'.'n~>46
32. "3""5oC)O
14.94O38OO
O. uOOO'.i' >O
O.OOOOOOu
O. OOOOO'. >(J
o. i"ioo(:>O(:»o
O.OOOOOOu
* BACK -HALF IMPINGER ANALYSIS WAS r
REQUIRED
Pr oqr am Re v i si on : 1 .•' i 0 •' 84
A-38
-------
lO I
E:IF-*=»
< iFc^UI
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
?3 o i j FC o IE:
T n o o s — s
O f^ 'T <=* >
FMC
POCATELLO ,
OUTLET 2-2
lO/2o/83
1244-1558
IDAHO
PARAMETER
VALUE
Si=ciTipling time
Etarometric Pressure ( i n . Hg )
Sampling nozrle diameter (in.)
Meter Volume (cu.-ft.)
Pressure (in.H20^
Temperature
Static Pressure < :i n . H2O )
Moisture Collected
Meter
Meter
Stack
Stack
St ac k
< g in)
Absolute stack pressure'in Hg)
Average stack temperature
-------
r-i E~ ~r M o o s s — s
PL ANT
Pl.MUl SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
E S "T
FMC
PGCATEL.LO , IDAHO
OUTLET 2-2
C-2
1O/26.-33
1244-1558
PARAMETER
RESULT
Vm (dsc-F )
Vm
Fl on (acmrn)
Frl ow
Flow .f?. 1O4
1117.715
121965
3454. O49
77922. 35
220
-------
O T f\ |N| S O LJ F< C3
E: F> *=» IM E: T &-i o o s
TEST
^ T X
PLANT
PLANT SITE
SAMPLING LOCATION
1 ESI #
DATE
TEST PERIOD
s._-0*=»o :
FMC
POCATELLO , IDAHO
OUTLET 2-2
1O/26/33
1244-1558
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsct
Grams/ac-f
Grai ns/dsc-f
Grains/scf
Grams/dscm
Grams / arm
Pounds .'dscf
Pound=/acf
Pounds-Mr
Ki 1 ocjr ?iTis/H
O. 187P7OO
OO25594
CO 1635 2
03^491 1
O. O 2
('). O9O3715
O. O577379
O . OOOOO56
O. OOOO036
26. 3S5O3OO
1 1 .96819OO
O. UOuOCiOO
O.OOOOOOO
'3. OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
'j. OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
BACH-HALF I WINGER ANALYSIS WAS NOT REQUIRED
Proqr am Rev i s i on : 1 •' 16 •
A-41
-------
r IE:
PLANT
PLANT SITE
SAMPLING LOCATION
TEST *
DATE
TEST PERIOD
FMC
POCATELLO ,
OUTLET 2-2
C-3
10/26/83
165O-1830
IDAHO
PARAMETER
VALUE
Sampling time (min.i
Barometric Pressure (in.Hq>
Sampling nozzle diameter (in.)
Meter Volume (cu.ft.)
Meter Pressure (in.H20)
Meter Temperature < F)
Stack dimension ( s-q . i. n . )
Stack Sl-ai-ic Pressure (in.H2O>
Stack Moisture Collected 6
4790.634
.42
321.369
25.78O88
142.719
6.64
16.88
76.4SOO1
23.7138
.'999
.84
A-42
-------
D I r=*|N| SOURCE
-1=* MI E: T no o s s —
IF" I !v|rtl|._
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO ,
OUTLET 2-2
C-3
10/26/33
165O-1S3O
IDAHO
PAPAMETER
RESULT
(dscf )
gas (sc:-f )
gas (scm)
moisture
Md
V 5 < -f p m )
Fl ow (ac f m)
Fl ow < acmm)
Fl ow rdsr-f m)
Fl. ow ( dscmm)
V. .[
V. EA
76.73636
2.173174
15. 17612
.4297878
16.51149
.8348351
29.73^6
27.79955
3816.623
1163.605
126972.5
3595.862
SCO 13.74
2266.13
93.33272
509.6532
Proaram Revision:1/1
A-43
-------
F-
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
METHOD S
L_o<^D
PMC
POCATELLO
OUTLET 2-i
IDAHO
10/26/83
165O-183O
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grsms
Gr ams/scf
Bre i ns/dscf
Gr ains/scf
Grems/ dscm
Grams/acm
Po'jnds /dsc-f
Pounds / ac-F
Poi.nds/Hr
Ki 1 oqrams/Hr
. 1431 3OO
0018652
,0011755
O2878O3
.0131 375
O6586O8
, O4 1 5058
O . OOOOO4 1
O.OOOOO26
1".746O8OO
8.956764O
0.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0. '.'OOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
'"'. OOOOOOO
0.OOOOOOO
BACK-HALF IhFIMGER ANALYSIS WAS NOT REQUIRED
Program Pe> i si on : 1/36-' 84
A-44
-------
IF-
so LI FS-
"F H O D
T E-I £3 "F
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
: FMC
: POCATELLQ , IDAHO
: OUTLET 1-1
: K -1
: 11/1/83
: O953-1235
PARAMETER
VALUE
Samp 1 i nq 11 me (rn i n . ) ^9
E'arometric Pressure ( i n . Hq ) 25.66
Sampling nozzle diameter (in.) .133
Meter Volume -93
Meter Temperature (F) 78
Stack dimension (sq.in.) 4242.92"
Stack Static Pressure (in.H2O) .65
Stack Moisture Collected (gm) 25O.377
Absolrtte stack pressure^in Hg) 25.7O78
Average shack temperature (F) 142.18
Percent- CO2 3.29
Percent 02 16.O7
Percent N2 75.65
Delps Subroutine result 24.&193
DGM Factor .9947
Pi tot Constant .34
A-45
-------
E:F=-
F^ I
PLANT
PLANT SITE
SAMPLINC9 LOCATION
TEST #
DATE
TEST PERIOD
r*l lEI T H O D S
FMC
POCATELLO
OUTLET 1-1
V -1
1 1 /1/83
O953-1235
IDAHO
PARAMETER-
V,T, (dsc-f )
Vm(dscm)
Vw qas
"/. moisture
Md
MWd
MW
'-'s <-fpm>
V=
Flow tdscmm)
". I
:. EA
49.24547
1.3^4632
11.80528
.3343254
19.33683
. 8O
-------
M IE T m O D
PLAN!
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FI1C
POCATELLO
OUTLET 1-1
H -1
11/1 '83
0953-1235
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/ dsc-f
Gr ams/a.cf
Gr ai n= .'dscf
Gr a i n= ' ac-f
LI r a iTi s / d £ c rri
Grams •' a cm
POI inds / d = c-f
Pounds ''a.c-f
Pound = • H»"
H i1oqrams/Hr
O.51134O1
(J . 01 O3835
O . CO A310(")
O.16O2173
O.O973634
O.3666412
O.2228063
O.OOOO229
O . OO<"iO 13 9
97.36O42OO
44.3892OOO
O.OOOOOOO
'">. OOOCiOOO
O. OOOO'.'OU
O. C'OOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
11. OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACi .-HALF IMFINGER ANALVSIS WAS NOT REQUIRED
Program Rev i si on : 1 / 16.'! '! '! '1
A-47
-------
SOURC
M E: T 1-1 o o '2.
o *=» T £=» >
PLANT
PLANT SITE
SAMPL ING LGCAT I ON
TEST #
DATE
TEST PERIOD
FMC
PuCriTELLO , IDAHO
OUTLET 1-1
h -2
11/1/33
\ 6U5-1947
PARAMETER VALUE
b 25.06
Sampling r.ozrle diameter (in. > ,1S3
Meter Volume .94
Meter Temperature 'Fl 80.33
Shack dimension <=q.in.'> 4242.^2"
Stack Static Pressure (in.H2O> .o5
Stack Moisture Collected 2o'J.352
Absolute st«c(. pressure ' i n Hq ) 25. ^'".i ""8
Average stack: temperature 1.38.i")A
Percent C02 7.94
Percent O2 16.18
Percent N2 75.88
Del ps Subroutine result 23,'"iO45
DGM Fact-or .^94 7
P i t o t Can n t ant .34
A-48
-------
I #=*tN4 £3 Ol. J FC C El
E: !=-*=»
iF' I INI (ft L
PL.AN T
PLANT SITE
SAI-1PL ING LOCAT I ON
TEST #
D^TE
TEST PEP IGO
TEST
FtEISO«_TS
PMC
POCATELLO , IDAHO
OUTLET 1-1
K-2
11/1/83
1605-1947
PARAMETER
RESULT
Vw gas (sc-f )
'-'w qas (sciTi
"•'. moi sture
Md
HWd
MW
'-..'= (-fpm)
'•-•'s (mpm)
Flow
-------
r-i
-------
f^f^G T rf^M SOLIRC
El F=- *=» M El T fr-i O D S
< IR rt W D *^ F *=* >
PLANT
PLANT SITE
SAMPLING LOCATION
TEST *
DATE
TEST PERIOD
"T ET.
FMC
PQCATELLO , IDAHO
OUTLET 1-2
K-3 (CORRECTED MOISTURE;
11 /I-2/83
22O&-O12S
PARAMETER
VALUE
Ssmplinq time (min.) ^6
Efarometnc Pressure ' i n . Hg ) 25.66
Sampling nozzle diameter . 9^
Meter Temperature 77.76
Stach dimension <=q.in.) 4242.927
Stacl-: Static Pressure (in.H20) .65
Stack Moisture Collected . 18
Delp=5 Subroutine result 23. 70^3
DGM Factor .9947
Pi tot Constant .84
A-51
-------
SOJJRCE TES
1-1 &' T M O D S 2: — S
PLANT
PLAN! SITE
SAMPLING LOCATION
TEST tt
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
OUTLET 1-2
K-3 (CORRECTED MOISTURE)
1 1 /I-2/83
2206-Ci 1 ^S
PARAMETER
RESULT
Vm (dscf )
Vm < dscm )
v'w ge.s
V. moisture
Md
MWd
MW
VB (mpm)
F 1 ow ( a c -f m >
Fl ow (acmrn)
Fl ow (dsc-f m)
Fl ow t dscrniTi)
v. I
". EA
46.
1.322229
12.63688
.3578^64
21.30OS3
.78o9^17
29.776
27.267o2
3853.493
1176.37
113689.6
3219.6,9
67991.37
1925.51
-------
El F>
PLANT
PL. -NT SITE
SAf'IPL ING I .GCAT I ON
TEST tt
D^TE
TEST PERIOD
OI-.JFCCE: TEST
METHOD 3
FMC
POCATELLO , IDAHO
OUTLET 1-2
K-3 (CORRECTED MOISTURE)
11/1-2/33
22O6-<")128
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dscf
Grams /ac-f
6r«i ns/dsc-f
Gr si n = - sc-f
Grams.dscrn
Grams/acm
Pounds/dsc-f
Fot.inds '' ac-f
Poijnds • Hr
Ki1oqrams/Hr
0.27198OO
(.). OQ58254
.OO34833
O898854
O.O537'554
O.2056^38
0. 123013°?
O.OOOO128
O.OOOOO77
c"'2. 4O< i7O<;)'j
23.7633OOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
0.OOOOOOO
* BACK-HALF IhPINGER ANALYSIS WAS NOT REQUIRED
Program Rev isi on: 1 / 1o '
A-53
-------
;
E: T E: i
PLANT
PLANT SITE
SAMPL ING L.OCAT I ON
TEST 4*
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
OUTLET i-2
L-l
1O/31 .'83
1S2B-2045
PARAMETER
VALUE
Sampling time
Meter Volume (cu.-ft.)
Meter Pressure (in.H20)
Meter Temperature (F)
Stack dimension (sq.in.>
Stack Static Pressure (,in.H2O)
Stack Moisture Collected (gm»
Absolute stack pressure'in Hg)
Average stact temperature (F)
Percent. C02
Percent O2
Percent IM2
Delps Subroutine result
DGM Factor
Pitot Constant
. 191
40.793
.•51
76.75
4242.927
.65
190.376
25.59779
136.34
1 6. 83
75.98OO1
17-9528
1.OO83
.34
A-54
-------
I iPiffxi SOURCE
METHODS 2:
I txJI#=U._ RESULTS
PLANT
PI AMI 'SITE
SAMPLING LOCATION
TEST 4*
DATE
TEST PERIOD
FMC
POCATELLO
OUTLET 1-:
L-l
1O/31 ''83
1828-2045
IDAHO
PARAMETER
RESULT
Vm
Vw gas (scf>
Vw qas < =cm)
"/'. tnoi sture
Md
MWd
MW
V= '-Fpm)
v's <,rnpm>
Fl ow (ac-f m)
PI ow (acrnm)
Fl ow (dsc-fm)
Fl ow
•; i
••'. EA
34.61O14
-C/8015C?1
8.976229
.2542O68
20.59412
. .7940589
29.828
27.39213
2921.218
390.6151
86O73
2437.588
51772.67
1466.2O2
1O3.18O1
521.2536
Program Revisions 1/1
A-55
-------
"F X CILJL..
PLANT
PL.ANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
SOURCE E:
HOD s
r E: i_ o f^, D
FMC
POCATELLO
OUTLET 1-1
L-l
1O/31/33
1328-2045
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams .'dsc-f
Grams/acf
Grai ns/dsc-f
Gr a i ns/ac-f
G r t3 iB = / d 3 C (Tl
Grains - a cm
Pounds/ dsc-f
Pounds /acf
Pounds/Hr
I- i i ograms/Hr
0 . 1 3'- >~77uO
O.OO37784
O.OO22727
O. u5833
O. '")35O67"T'
O. 1334143
0.0802434
O.OOOOO83
0. '-'O'" "I'^itj
25.88OO6OO
11.73^1200
0. <.)OOOOO'".>
0. (.>i">OOOO-O.
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O. oouOO'~>o
i") „ OOOOOOO
• ). c.iOOOO'.iO
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Kevi =i on ; 1 /
S4
A-56
-------
EZ ff=- ,
METHOD ^2. — '
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
PMC
POCATELLQ
OUTLET 1-2
L-2 (CORRECTED
11/1/83
0942-12O3
IDAHO
MOISTURE)
PARAMETER
VALUE
Samp 1 i nq t i me (mi n . ~> 96
Barometric Pressure
-------
I f^t^H SOURCE
rt E: ~r m CD E> s s
PLANT
PLANT SITE
SAMPLING L OCATI ON
TEST #
DATE
TEST PERIOD
T EEIS
FMC
POCAFELLO , IDAHO
OUTLET 1-2
L-7: (.CORRECTED MOISTURE)
1 1/1/83
0*542-1203
PARAMETER
RESULT
Vm (dsc-f >
^m(dscm)
Vw gas (sc-f )
Vw gas (scm)
"'. moi sture
Md
MWd
MW
V s < -F p m)
Vs
': I
'•. EA
36.82282
1.O42822
C?.6OO471
.2V18853
20.6802^
.7^31971
2':?.8
-------
^ #=» T3 I #^ r^ S O K_J F< O El
r F • #=* 1-1 IE: nr H o D ^s
PLr-NT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
7- El S T
PMC
POCATELLO , IDAHO
OUTLET 1-2
L.-2 (CORRECTED MOISTURE)
11 - 1/93
0942-1203
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dscf
Gr arns./ect
Grai ns .'dscf
Grai ns/' acf
Grams/dscm
Founds' dsc-f
Pounds/ac-f
Founds .-'Hr
Ki1ograms/Hr
O.1^76200
O.OO53o68
O.OO32386
O.OS28O94
O. O4W71?
O.18^5010
O. 1 1.43557
O . (>OOO1 1 8
<">. OOOOO7 1
3v.62537OO
1 7 - 9739500
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revision:I/lo<
A-59
-------
E IF- *=*
.ft INI
ME
so u j Ft
HOD
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
OUTLET 1-2
L-3 (CORRECTED
11/1/33
1524-1747
IDAHO
MOISTURE)
PARAMETER
VALUE
Sampling time (min.) 96
Barometric Pressure 219.1517
Absolute stack, pressure (in Hg) 25.7O78
Average stack temperature 135.65
Percent CQ2 7.73
Percent O2 16.72
Percent N2 75.55
Delps Subroutine result 2O.7298
DGM Factor 1.OO33
Pi tot Constant .34
A-60
-------
Ft *=» D I #=» IM
F- I
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
Ft EE S U 8_ T :
FMC
PQCATELLQ , IDAHO
OUTLET 1-2
L-3 (CORRECTED MOISTURE.)
1 1/1/83
1524-1747
PARAMETER
RESULT
Vm ', dsc-f )
Vm
Fl ow ( ac-f m)
Flow < acmm)
F1 0^ < d sc -f m)
Flow(dscmm)
•: i
•/. EA
39.63241
1. 12239
1 0 . 333
. 2926307
20.63031
29.9056
27.44349
3362. 706
1025.2.15
9908 1 . 36
2S05. 984
59857.55
1695. 166
102. 1938
518. 4173
Program Revisions 1- 16/
A-61
-------
PI-AMI
PLANT SITE
SAMPLING LOCATION
TEST *
DATE
TEST PERIOD
S O LJ R: C E
Ml E T l-l O H> S
FMC
POCATELLO
, IDAHO
OUTLET 1-J
L-3 (CORRECTED MOISTURE)
11/1/83
1524-1747
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Ljrams
Grams/dset
Grams/act
Grai ns/dscf
Grai ns/ac-F
Grams/d=cm
Grams ''acm
Founds/'dsc-f
Pounds/act
Pounds/Hr
Ki1oqrams/Hr
O.12711OO
O.OO32072
0.001^376
O.04^4875
0. O2':?8O<">O
U . OOU'.l'.X.'U
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O . OU'JOUUU
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revi si on : 1 / Its/ 84
-62
-------
R rt O I #^ INI SO IJ R C El
E: *='#=* r-S El T HI O D S —
< F< f=* UJ D ^
PLANT
PLANT SITE
SAMPLING LGCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
INLET 2-2
A 1-1
1O/27/33
1445-1515
PARAMETER VALUE
Sampling time -8.15
Stack Moisture Collected
-------
PLANT
F'LANT
#=* D I ^ IMl SOURCE!
=* r-H El ~T H O D S 2:
FMC
POCATELLO
INLET 2-2
A 1-1
1O/27/83
1445-1515
TE
SAMPLING LOCATION
TEST tt
DATE
TEST PERIOD
IDAHO
PARAMETER
RESULT
'v'm
V'w gas 'scm)
"'. moisture
Md
MWd
MW
Vs (-Fpm)
Vs (mpm)
Flow(acfm)
Fl ow (acmm.i
F] ow
-------
E F-
METHOD 5
PLANT
PLANT SITE
SAMPLING LOCATION
TEST tt
DATE
TEST PERIOD
FMC
POCATELLQ
INLET 2-2
A 1-1
1O/27/83
1445-1515
I DAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dscf
Grams/ac f
Gr ai ns/dsc-f
Gr ai HE /ac-f
Gr am=. / dscm
Grams/acm
Pounds .''d:?cf
Pounds -acf
Pounds/Hr
Kilograms/Hr
O
O
O
483
O.243790O
O.O39O657
0.0161398
O.6027836
O.2490368
1 .37941OO
5698956
OOOO861
OOOO356
2409OOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
219.1966OOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMP1NGER ANALYSIS WAS NOT REQUIRED
Program Revisions 1/1
A-65
-------
TEST
E: T IM O D 2: —
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , ID.
INLET 2-2
A 1 -2
10/27/33
1655-1736
iHO
PARAMETER
VALUE
Sampling time -8.15
Stack Moisture Collected 25.16O74
A-^erscje stack temperature (Ft 547
Percent CO2 7.6
Percent O2 16.4
Percent N2 76
Delps Subroutine result 31.0733^
DGM Factor 1.0083
Pi tot Constant .84
A-66
-------
Fc *=% D X
I lNJ^L_ Ft
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
TS
FMC
POCATELLO
INLET 2-2
A 1-2
1O/27/33
IDAHO
PARAMETER
RESULT
Vm (dsc-f )
Vm
Ww gas < sc-f i
Vi-j qas (scrn)
V. moi st. ure
lid
MW
'«' 5 < i p iTl )
V5 UTiplTl)
PI ow < ac Fm '
Fl ow (acmm )
Fl ow
-------
METHOD
I O <
PLANT
PLANT SITE
SAMPLING LOCATION
TEST tt
DATE
TEST PERIOD
FMC
POCATELLG
INLET 2-2
A 1 -2
10/27/83
1655-1736
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams/acf
Grai ns/dsc-f
Grai ns/ac-f
Grams/dscm
Grams/acm
Pot.inds/dscT
Pounds/ac-f
F'ounds/Hr
Ki1ograms/Hr
O.473120O
0.O466264
O.013^361
0.7194461
0.292^553
1.64638OO
O.6VO3986
O.OOO1O28
O.OOOO4 1 9
43O.2753OOO
19S.1718OOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
("I. OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Kevisi on: 1/16/84
A-68
-------
I #^»M SOURCE TEST
METHOD S —S
PLANT
PLANT SITE
SAMPLING
TEST tt
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
viTION INLET 2-2
A 2-1
10/28/33
1OO7-1O53
PARAMETER
VALUE
Sampling time (min.) 30
Barometric Pressure (in.Hg) 25.68
Sampling nozzle diameter (in.) .122
Meter Volume (cu.-Ft.) 9.538^99
Meter Pressure (in.H2O) .28
Meter Temperature
-------
=* (-I EI ~T H O D S S
IR- I iNlft l_ RESULTS
PLANT FMC
PLANT SITE POCATEI.LO
SAMPLING LOCATION INLET 2-2
TEST # A 2-1
DATE 10/28 ''83
TEST PERIOD 10O7-K'>53
IDAHO
PARAMETER
RESULT
'•Jm (dscf i
Vm(dscm>
Vw qa= (sc-f )
Vw gas '. moisture
Md
MWd
MW
'-/' = < -f p m >
Vs (mpm)
Fl ow (ac-f m)
Flow(acmm)
Flow
Flow(dscmm)
v. I
•'. EA
7.931316
.2246149
.5969SO8
.O169065
7.OOOOO1
. 93
29.613
23.SO474
7O33.319
2145.629
243O9Q.S
6884.332
1O3797.5
2939.546
103.4289
Program Revision:1/16/84
A-70
-------
FS ft D i ft rxi
E: F> ft Ifl EI ~T H O D
=• ft Ft T T C l_J L_ ft T I
PLAN r
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
L_OftD I rslCB
FMC
POCATELLO , I.Dr--HO
INLET 2-2
A 2-1
10/28/83
1O07-1O53
PARAMETER
FRONT-HALF
TRAIN TOTAL
To^el Grams
Gt =>.ms/dscT
Grams/acf
Grai ns/dsc-F
Gr si ns /ac-f
Grams/dscm
Grsms/scm
PoundE/dscf
Pounds/ac-f
Pounds/Hr
I- i 1 oqrams/Hr
0
O
o
1
o
o
o
568
. 32S5OOO
0414131
.0176351
6390812
.2728813
462473O
.6244625
OOOO913
,OOOO39O
77O3OOO
O.OOOOOOO
0. OOOOOt'K")
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
u. """"
257-99^
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IHPINGER ANALYSIS WAS NOT REQUIRED
Program Revisi on: 1/lc
A-71
-------
ift D I *=* IM SOURCE!
» METHOD S —'
FhC
POCATELLO
INLET 2-2
/i •-.•• _ ^
!~1 .ii. *L.
10/28/33
H HCTCr -1 -i ^-. l=-
1 1 ,_l -...I — 1 J_ ^ ,-l
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
I DAHG
PARAMETER
VALUE
i nq t i me ', m i n , )
Barometric Pressure ( i n . Hq )
Sampling nozzle diameter (in.)
Meter Volume (cu.-ft.)
Meter Pressure
(F>
3O
25.63
.175
1 3 . OO2
.435
1C 1.3
4'r''73.5
3.15
14.3O28
25.(">8C>74
4/6.5
5.71
17.61
76.68
29.O3135
1 . OO83
.84
A-72
-------
E: T 1-1 0
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-2
« 2-2
1O/2S''33
11.55-1225
IDAHO
PARAMETER
RESULT
'•••'m (dsc-f )
VtTi
Vs ', mprn)
Fl ow ( ac fin )
Flow(acmm)
Fl ow (dsc-f rn >
Fl ow (dscrnrn)
"'. 1
"'. EA
8.959579
.2537353
.674377
1.909836E-O2
7.OOOOO1
. 93
29.613
28.8O474
4653.914
1418.876
160737.8
4552.O94
7O648.95
20OO.778
87.46054
6&8.6873
Program Revi si on: I/lc
A-73
-------
SQLJFSCI
T
F> KG* R: r
PLANT'
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATEL.L.O , IDAHU
IMLET 2-2
H 2-2
10/28/33
1155-1225
PARAMETER
Total Grams
Grams/dsc f
Gram5/act
Grai ns/dsc-f
Grai ns/ac F
Grams/dscm
Grams/acm
Pounds/dsc-f
Pounds/act
Pounds/Hr
K 11 ograrns/Hr
FRONT-HALF
TRAIN TOTAL
0.
O.
O .
O.
O.
1.
O.
O.
O .
329.
149.
31545OO
0352O81
O15475O
5432615
2387793
243199O
5464224
OOOO776
OOOO34 1
O8530OO
27210OO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
'.'. OOUOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Pr oq r am Rev i s i on : 1 / 1
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
lEITHOD ^i — ^z
PMC
POCATELLO
INLET 2-2
A 3-1
K>/29/83
152O-1550
TEST
IDAHO
PARAMETER
VALUE
Samp ling t i me < rn i n . >
Barometric Pressure (in.Hq)
Sampling nozzle diameter
St. ac^ dimension (sg.in.)
Sti.cl Static Pressure
Sfcac^: Moisture Collected (qm)
Absolute stack pressure(in Hq>
Average stack temperature (F)
Percent CO2
Percent O2
Percent N2
Delps Subroutine result
DGM Factor
P i t o t C o n s t a n t
3O
25. 68
. 122
9.135001
.275
1 O6. 2
4973.5
-8. 15
20.86757
25.O8O74
565
9.67
14.96
48.O1652
I. . OO83
.34
A-75
-------
EE F='
F I
PL. ANT
PLANT SITE
SAMPLING LOC
TEST #
DATE
TEST PERIOD
"TEST-
1O/2S/83
152O-155O
PARAMETER-
RESULT
ViTl (dsc-f )
Vm(dscm)
Vw gas (sc-F )
Vw gas (scm)
7. moisture
Mel
MWd
MW
V= (-fpm)
'-.'s (mprn)
Flow(ecfm)
Fl ow (acrnm)
Fl ow(dsc-f m)
Flow(dscmrn)
/'. I
7. EA
7.418366
.21OOSS1
,933^06
2.786422E-0:
11.71
.8829
30.1456
j^8 • ' jj !.< j»._'
77OS.128
235O.O39
266224.8
7539.487
101496
2874.366
103.7161
3O2.9763
Program Rev i si on: 1/16 /34
A-76
-------
• #=% r-i E T H o o s
T. C LI L_^TEI l_O*=»E>I
FMC
PLANT
PLANT SITE
SAMPLING LOCATION
TEST 4*
DATE
TEST PERIOD
POCATELLO
INLET 2-2
A 3-1
tO/28 .'33
1520-155O
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams /dsc-f
Grams /acf
Grai ns/dscf
Gr ai ns/ac-f
Grams ' dscm
Gr ams./acm
Pourids ' cisc-f
Pounds /Mr
Ki 1 ogr ams /Hr
0. 4O4. OOOOOOO
0.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Pev\si on: 1/16
A-77
-------
M
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
SOURCE TEG
THOD S—S
FMC
POCATELLQ , IDAHO
INLET 2-2
A 3-2
1O/28/83
1727-1757
PARAMETER
VALUE
Sampling time (min.i
Barometric Pressure ( i n . Hq )
Sampling nozzle diameter (in.)
Meter Volume ecu. ft.)
Meter Pressure (in.H20)
Meter Temperature (F)
Stack dimension (sq.in.)
Stack Static Pressure (in.H2O)
Stack Moisture Collected
Percent C02
Percent O2
Percent N2
Delps Subroutine result
DGM Factor
Pi tot Constant
3O
25.68
.175
1C. 254
.4?
1O4
4973.5
-8.1.5
23.4OO1. 7
25.'J8'".i74
611
9.67
14.96
75.37
33.282O1
J . OO83
.34
A-78
-------
f* D I
S O L J t=* C E=l
f= X
PLANT
PI i-iNT SITE
SAMPLING I..OCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-2
A 3-2
10/28/33
1727-1757
I DAHG
PARAMETER
RESULT
viTi (dscm)
Vw gas
Vs ( mprn'
Flow(actm)
Fl ow (scrum)
Flow
-------
#=k D I f* |N| SOURCE! TEST
i* METHOD S
CUL_*=*TE l-O^D ~L
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-2
IDAHO
10/23/83
1727-175
PARAMETER'
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams'dsct
Grams/ac-f
Gr ai ns / dsc-f
Grai ns/ac-f
Grams/dscm
Grams/acm
Pounds/dsc-f
Paiinds/ac-f
Pounds-Hr
K i 1 o q r a. m s / H r
(_)
O
o
o
o
1
o
o
o
317
, 29677QO
0356751
,013016^
5504661
,2OO846"
4596 ISO
OOO0787
OOOO287
7799OOO
144.144OOOO
O.OOOOOOO
("). OOOTlOOO
O.OOOOOOO
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
INLET 2-1
B 1-1
10/27/83
135O-1545
PARAMETER
VALUE
Campling time (min.) 39
Barometric Pressure < i n . Hg ) 25.76
Sampling nozzle diameter (in.) .122
Meter Volume 11.5"
Meter Pressure 113.2
Stac^' dimension (sq.in.) 4973.5
Stsci.- Static Pressure (in.H2O) -3
Stack Moisture Collected
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
I f=*t^ SOURCE
METHODS S —
RESULTS
FMC
POCATELLO
INLET 2-1
B 1-1
10/27/83
1350-1545
1DAHO
PARAMETER
RESULT
'v'm (dsc-F i
Vrn (dscm)
'^•'w qas < sc-f )
Vw gas <,scm)
V. moi sture
ttd
MWd
MW
V s < f p m)
VS (lTlpiTl>
Flow
2. 107254E-0:
7.51'r?
-------
r> i
METHOD
r i cut-
PLANT PMC
PLANT SITE POCATELLO
SAMPLING LOCATION INLET 2-1
TEST # B 1-1
DATE 1O/27/33
TEST PERIOD 135O-1545
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams' dsc-f
Grams/ac f
Grai ns/dsct
Gr ai ns /ac:-f
Grams'dscm
Gr amsX-sciTi
Pound s/dsc-f
Pounds/acf
Poi-inds/Hr
(• i 1 ograms/Hr
O.O7O01OO
O.OO765O8
O.OO30574
O. 11 BOS16
O.O471751
O.27014^3
O.1O79554
O.OOOO16^
O.OOOO067
7f5. 63.t)' tOOO
34.3OQ26OO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMPINBER ANALYSIS WAS NOT REQUIRED
Program Revisi on: 1/16-
A-83
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
SOURCE!
METHOD s —
FMC
POCATELLO
INLET 2-1
B 1-2
10/27/93
19OO-193O
I DAHO
PARAMETER
VALUE
Sampling time (nun.)
Barometric Pressure (in.Hq)
Sampling nozzle diameter (in.>
Meter Volume (cu.-ft.)
Meter Pressure 3211
25.31 177
555
8.55
15.84
75. ol
22. 75 13^
. 995
.84
A-84
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TET3T #
DATE
TEST PERIOD
FC E: s«_
PMC
POCATELLO
INLET 2-1
B 1 -2
10/2'7/83
I'^OO—1930
I DAHO
PARAMETER
RESULT
'w'ni (dsc-f >
Vm <,dscm)
Vw gas
'•^'w gas <5cm)
/'. moi sti.irs
Md
MWd
MW
Vs
Vs (.mpm)
Flow(acfm)
Flowiacmm)
Fl ow (dsc-f m>
FT ow(dscmm)
">'. I
•/. EA
9. O6419r-?
.2566981
.737054
2.O87337E-02
7.519997
.9243OO1
3O. O'.'>16
29.O99Q8
3612.O44
11O1.233
124753.5
3533.019
50772.58
1437.879
116.3755
384.369
Program Revision: I/16.-3-1
A-86
-------
R^D T *=*|NJ SOLJFt
El F> #=* M EE ~T »-i O O
I Ci: LJ L_ f* T E: L
PLANT FMC
PLANT SITE POCATELLO
SAMPLING LOCATION INLET 2-1
TEST tt B 1-2
DATE 10/27/33
TEST PERIOD 190O-1930
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams /dsc-f
Grams/ac-f
Gr ai ns/dsc-f
Grai ns/acf
Grams/dscm
Grams/acm
Pounds/dsc-f
Pounds/acf
F'-unds/Hr
Ki1ograms/Hr
0.O6585OO
OO72648
,O029567
1120966
,0456214
256521V
,1O44OOO
00CO 160
,OOOOO65
79950OO
(.1,
0
O
o
l")
o
o
o
43
I. 13531OO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O. OOOOOO<)
O.OOOOOOO
O. OOOOOO''
O.OOOOOOO
O.OOOOOOO
O. OO<_>OO<.'< i
O . i.»".iOOOOO
0.OOOOOOO
BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revision
A-86
-------
SOURCE
r-i e: T m o D s —
TEST-
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
INLET 2-1
B 2-1
1O/29/S3
PARAMETER
VALUE
Sampling time .183
Meter Volume (cu.ft.) ID.839
Meter Pressure (in.H2O) .315
Mei-er Temperature 95.8
St.ack dimension (sq.in.) 4973.5
Stack Static Pressure (in.H2O) -8.15
Stack Moisture Collected O74
Average stack temperature (F) 5O7
Percent C02 7.15
Percent O2 16.69
Percent N2 76.16OO1
Delps Subroutine result 22.74478
DGM Factor .995
F i tat Const ant .84
A-87
-------
EEF=-
F=" I
PLANT-
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
_ RESULTS
FMC
PDCATELLG
INLET 2-1
B 2-1
1C' 28''S3
1056-1127
IDAHO
PARAMETER
RESULT
Vm (dsc-f )
Vm(dscm)
Vw gas <5c-f )
Vw gas (scm)
"/. moisture
Md
MWd
MW
Vs (-f pm)
Vs iffipm)
Flow(acfm)
Fl ow (acfnm)
Flow(dsc fm)
Flow(dscmm)
'/. I
'. EA
8. C?O324699c?
29.8116
28.^2219
3625.678
1105.39
125224.4
3546.354
5333O.36
1511.732
101.SO39
488.5485
Program Revisi on: 1/ 16/84
A-88
-------
F< *=* O T <=» 1-4 SOURCE: T IE £3 "T
! -1E T H O O S
I C; H .1 L_ #=» T EZ L_ CJ #=k E> I IMG
FMC
POCATELLO , IDAHO
INLET 2-1
B 2-1
1O/28/83
lO5o-1127
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Gram's/d = c-f
Grams/acf
Gr ai ns/dsc-f-
Grain=/ac f
Grams /dscrn
Grams/acm
Pounds/dsc-f
Pounds /ac-f
Pounds/Hr
K i1oqrems/Hr
O.O9583OO
-------
R f=* D I #=* h4 SOURCEZ
EZ F> e* i-i E: ~r MI o D s —!
PMC
POCATELLG
INLET 2-1
B 2-2
1O/23/83
1245-1315
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
IDAHO
PARAMETER
VALUE
Samp ling t i me < m i n . >
Barometric Pressure ( i n . Hg )
Sampling nozzle diameter (in.)
Meter Volume ten. ft.)
Meter Pressure
Absolute stack pressure < in Hg )
Average stack temperature (F)
Percent CO2
Percent O2
Percent N2
Delps Subroutine result
DGM Factor
P i t ot Con = t an t
3O
25.86
.122
5.045
.055
1O4.8
4i:?".73.5
8.15
7.OO6O1
25.26O74
4"O
7.15
16.6
-------
I f^t^t SOURCE
METHODS S
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-1
B 2-2
10/23/83
1245-1315
IDAHO
PARAMETER
RESULT
TI (dscm)
Vw gas
"••'. moi sture
Md
MWd
MW
Vs< Fpm)
Vs (mpm)
Fl ow (ac-f m)
Fl ovi (acmm)
F 1 ow < d sc f m )
Fl ow (dscmm)
'•'. I
••'. EA
4.O56564
.1148819
.33O3334
^.35504lE-0'
7.53
. 9247
2^.8116
23.^2219
5373.412
1639.76
13576O.6
5260.741
3O6O2.65
2282.667
71.416O4
488.54S5
Program Revi =i on : 1 / 16 • S-
A-91
-------
i
SOLJRCEZ -TEES-T
EE F> *=» r*i EE i
r :r oui_*=*n
PLANT
PL.ANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-1
B 2-2
1O/23/S3
1245-1315
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams-' ac f
Gr ai ns/dsc-f
Grai ns/acf
Grams/dscm
Grams •'acrn
Pounds •'dsc-f
Pounds/acf
Pounds/Hr
Ki1ograms/Hr
O.08154CO
O.02O1OO8
0.0087218
O.31O1547
O.134573O
0.7097578
0.3O79682
O.OOOO443
O.OOO0192
214.34910OO
^7.228O9OO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HAL.F IMPIWGER ANALYSIS WAS NOT REQUIRED
Program Revisi on: 1/16/S4
A-92
-------
C #=* D I #=* ih4 SOURCES TEST
METHOD S—3
O^T«=» >
FMC
POCATELLO , IDAHO
INLET 2-1
B 3-1
1O/23/33
1525-1555
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
PARAMETER VALUE
Samp 1 i nq t i me < m i n . "> 3O
Barometric Pressure ( i n . Hq *> 25.68
Sampling nozzle diameter 1O6.2
Stack dimension < sq . i n . i 4':''73.5
Stack Static Pressure <:tn.H2O) -8
Stack Moisture Collected fgm) 22.0334^
Absolute stack pressure(in Hq) 25.O917T
Average stack- temperature (F) ^O5
Percent CO2 10.3
Percent 02 14.64
Percent N2 75.O6
Delps Subroutine result 21.5196-
DGM Factor .995
P i t at Con = t => n t. .84
A-93
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
SOURCE
METHODS 3: —
RESULTS
FMC
POCATELLO
INLET 2-1
B 3-1
1O/2G/83
IDAHO
PARAMETER
RESULT
Vm(dsc-f )
Vm(dscm)
Vw gas
Fl ow
v. I
'. EA
8-—\ i ^ —r'~t'-\
• jL-O 1 / ^.^.
.233^72
1.O38876
2.C?42098E-0:
11. 16C?(:?9
.3883
3O.2336
28.86711
3445.2O1
1O5O.366
113991
3369.826
43946.86
1244.575
118.':r.624
282.S527
Program Re /i si on : 1 / .1
A-94
-------
F<(^r> i
F=- *=* R ~T I C L.I L_ #^» T El
PLANT
PLANT SITE
SAMPLING LOCATION
TEST tt
DA FE
TEST PERIOD
l_O#=*D I
FMC
POCATELLO ,
INLET 2-1
B 3-1
1O/23/33
I DAHO
PARAMETER'
FRONT-HALF
TRAIN TOTAL
Total Gr^iTis
Grams/d = c f
Grams/ac-f
Grai ns/ dsc-f
Grsi ns/ac f
Grams/dscm
Grams-'acm
Pound s/dsc-f
Poijnds/acT
Pounds/Hr
Ki1oqrams/Hr
O.11843OO
O.0143343
O.OO52943
0.2211857
O.O8169O3
O.5O61613
O.13694O1
0.OOO0316
O.OOOO117
83.344S6OO
37.8O498OO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Rev i si on : 1 / 1 o •• 8
A-95
-------
=» METHOD S —S
PLANT FMC
PLANT SITE POCATELLO
SAMPLING LOCATION INLET 2-1
TEST # B 3-2
DATE 1O/28/33
TEST PERIOD 1719-1751
IDAHO
PARAMETER
VALUE
Sampling time (min.)
Barometric Pressure
C02
02
Percent
Percent
Percent N2
Delps Subroutine result
DGM Factor
Pi tot Constant
25.68
. 122
20.^61
1.2
111.2
4^73.5
8. 15
44.28O86
25.O8O74
5^1.5
10. 3
14.64
75. O6
32.45661
- 995
.34
A-96
-------
I *=*|v| SOURCE
METHODS rs
TEST-
PLANT
PL-ANT SITE
SAMPLING L OCAT ION
TEST #
DATE
TEST PERIOD
FMC
PQCATELLQ
INLET 2-1
B 3-2
1O/2S/33
1719-1751
IDAHO
PARAMETER
RESULT
Vm'. moisture
Md
MWd
MW
Vs '.-f pm)
v's . t
A-97
-------
R: £* D I «^t N S O «_J Ft G E:
* M E: ~r 1-1 o E> s
PI..ANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
INLET 2-1
B 3-2
10/28/33
171P-1751
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grarns./dscf
Grams/act
Grai ns ''dsc-F
Gr ai ns/ac-f
Grams/dscm
Grams/acm
Pounds/dsc f
Pouinds/ac-f
Poi.inds/Hr
Ki1ograms/Hr
0.1213300
<"i. OOV3O74
O.OO27323
O.1127536
O.04215^3
O.258O252
O.0^64773
O.OOOO161
O.OOOO06O
o4.88793OO
29.432^7OO
/ 84
A-98
-------
P: f=* o i f* INI SOURCE: TEST
E f=- <=* METHOD :2 —• S
PLANT PMC
PLANT SITE POCATELLO , IDAHO
SAMPLING LOCATION OUTLET 2-2
TEST * C-A-1
DATE 1O/26/83
TEST PERIOD O85O-1O44
PARAMETER
VALUE
Sampling time (min.)
Barometric Pressure (in.Hg)
Sampling nozzle diameter (in.)
Meter Volume (cu.ft.)
Pressure
dimension ( sq . i n . )
Static Pressure
-------
E: F=-
.ANT
.ANT SITE
itIPLING LOCATION
:BT #
iTE
:ST PERIOD
PMC
POCATELLO
OUTLET 2-:
C-A-1
1O/26/83
O85O-1044
IDAHO
PARAMETER
RESULT
Vm(dsc-F)
v'm (dscrn)
Vw gas < 5C-f )
Vw gas (scm)
"/. moisture
Md
l"1Wd
MW
Vs (-fpm)
Fl ow < ac-f m)
Fl ow ( acmm)
Fl ow
-------
El IF- #=»
T H O D
Z CLJL_,
PI ANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
OUTLET 2-
C-A-1
10/26/83
O35O-1O44
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams /dsc-f
Grams / ac-f
Grai ns • dsc-f
Grai ns/ ac-f
Grams/d s c m
Gr am= / acm
Pounds/'dsc-f
Pounds /ac f
Pounds •' Hr
Ki1ograms/Hr
0.O1477OO
O.GOOS574
O.OOO5565
O.01322^5
O.OO85S61
030 2743
01964S5
O.OOOOO1^
0.GOOOO12
<9. 4448 190
4.2341420
0.OOOOOOO
O.GOGOOOO
O.OGGGGGG
0.OOOOOOO
O.OGGGGGG
O.OOOOOOO
0. OO'">OOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
0.GGOOOOG
* BACh-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Rev i si on:1/16'
A-101
-------
Ft £* o I ift M £3 O 3 J Ft i
* r-i IE: T n o D
PLAINT
PLANT SITE
SAMPLING, LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
OUTLET 2-:
C-A-2
1O/26/83
13O6-1548
IDAHO
PARAMETER
VALUE
Sampling time
Meter Pressure (in.H20)
Meter Temperature (F)
Stack dimension
Stack Shatic Pressure
-------
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO
OUTLET 2-:
C-A-2
10/26/83
13O6-1548
IDAHO
PARAMETER
RESULT
Vm Cdscm,'
Vw gas <5c-f )
Vw gas (scm)
"/. moisture
Md
MWd
MW
v s < -f p m )
Fl ow
-------
MIEZTHOD
R- £=» F< T I 0 LJ L
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
LOrftD I r-4C3
FMC
POCATELLO , IDAHO
OUTLET 2-2
C-A-2
10/26/33
13O6-1548
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams/ac-f
Gr ai ns /dsc-f
Grai ns/ec-f
Grams/dscm
Grams/acm
Pounds/dscf
Poi..inds / act
F'O'jnds/Hr
Ki 1 oqraiTis/Hr
O. O43650(J
O. OO2261S
O. CO 144 35
("). 0349OO2
0. 0222726
O. O798656
0 . O5O9686
O. OOOOO5O
O . OOOOO32
O .
O.OOOOOOO
O.OOOOOoO
O.OoOOOOO
O. OOOOOCiO
O . O( )OOO'"><")
1O. 93t>l 10O
* BACK-HALF IMPINGER ANALVSIS WAS NOT REQUIRED
Program Revision:1/16/84
A-104
-------
Ft ift D I *2»fxl SOLJFcCE
E f=- <=* METHOD 2: —
PLANT
PLANT SITE
SAMPLING LGCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO , IDAHO
OUTLET 2-2
C-A-3
1O/26/33
1642-1816
PARAMETER
VALUE
Sampling time (min.) 6O
Barometric Pressure
-------
SOURCE:
METHODS S
PLANT
PLANT SITE
SAMPLING LOCATION
TEST •*
DATE
TEST PERIOD
TEST
FMC
POCATELLO , IDAHO
OUTLET 2-2
C-A-3
1O/26/83
1642-11316
PARAMETER
RESULT
V
Flow /84
A-106
-------
METHOD
C CLJL.
PLANT
PLANT SITE
SAMPLING LOCATION
TEST 4*
DATE
TEST PERIOD
L_Orf=»D ]
FMC
POCATELLO , IDAHO
OUTLET 2-2
C-A-3
1O/26/33
1642-1816
PARAMETER
FRONT-HALF
TRAIN TOTAL
Grams
Grams/ dsc-f
Grams/ac-f
Grai ns/dsc-f
Grai ns/acrf
Grams/dscm
Grams/acm
p.-unds/dscf
Pounds/acf
PoLinds/Hr
Ki1ograms/Hr
O.O251^OO
O.GO 14948
0.OOO942S
O.O230654
O.O145475
O.O527828
0.O3329O5
O.OOOOO33
O.OOOOO21
16.6942OOO
7.5724390
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O. OOO<"'OOO
BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revisi on:1/16
A-107
-------
T H O D S —
D^
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
PMC
POCATELLO .
OUTLET 1-1
K-A-1
10/31/83
17O3-1845
IDAHO
PARAMETER
VALUE
Sampling time 67.45146
Absolute stack pre=sure 141.5
Percent CO2 8.28
Percent O2 16.O?
Percent N2 75.65
Delps Subroutine result 25.34389
DGM Factor .9947
Pi tot Constant ,,34
A-108
-------
i #=*IM SOURCE:
METHODS ^
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
PQCATELLO , IDAHO
OUTLET 1-1
K-A-1
1O/31/83
1703-1845
PARAMETER
RESULT
Vm (dsc-f )
Urn (dscm)
Vw gas
-------
i #=*r-j SOURCE:
METHOD S
O *=% D
TEST-
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO ,
OUTLET 1-1
h.-A-l
10/31/83
1703-1(345
IDAHO
PARAMETER
FRONT-HALF
TRAIN TOTAL
Total Grams
Grams/dsc-f
Grams/acf
Grai ns/dsc-f
Grai ns/acf
Grams/dscm
Grams /scm
Pounds/dsc-f
Pounds/ac-f
Pounds/Hr
Ki 1 oqrarns/Hr
O.O5O97OO
O.O03S674
O. OO234C?8
0.0596739
O.O362581
1365577
0829731
0.OOOOOS5
O. OOnOi'i52
37.524210O
1 7.O2OS70O
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
("). OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Program Revi si on: 1/16/84
A-110
-------
MI IE: T n D r> s
PLANT
PLANT SITE
SAMPLING LOCATION
TEST #
DATE
TEST PERIOD
FMC
POCATELLO ,
OUTLET 1-2
L-A-1
1O/31 /83
1526-1651
IDAHO
PARAMETER
VALUE
Sampling time (min.l
Barometric Pressure (in.Hg)
Sampling nozzle diameter —, a -~t — r
^.^r^, • ~i ^- /
.65
31.52677
25.5977^
1 36 . 3
7.2
16.83
75 . 980O 1
18.49777
.84
A-lll
-------
R: #=n O I ^ r^l SOURCE
E: R- *=* METHODS s
F- I INJ «s» l_ RESULTS
PLANT
PI..ANT SITE
SAMPLING LOCATION
TEST $
DATE
TEST PERIOD
PMC
POCATELLO , IDAHO
OUTLET 1-2
L-A-1
10/31/33
1526-1651
PARAMETER
RESULT
Vm(dsc-f )
Vm (dscm)
Vw gas
Vw gas (scrn)
"/. moi st. ure
Md
MW
Vs<-fpm>
Us
Flow (dsc-f m)
Fl ow < dscmm)
". I
••'. EA
14.79805
.41908O6
3.343988
.1O83617
20. 62
. 7938
29.823
27.389O7
3O1O.061
917.7O16
SS69O.75
53233.75
1509.137
168.085
cr '-i H <—. cr i—i i
J J-. 3 m ±. ' O O
Program Revision:1/16/84
A-112
-------
El F-
r-1 E ~T H O O
PLANT
PLANT SITE
SAMPLING LOCATION
TEST tt
DATE
TEST PERIOD
I IMC3
FI*IC
POCATELLO , IDAHO
OUTLET 1-2
L-A-1
10/31/33
1526-1651
PARAMETER
FRONT-HALF
TRAIN TOTAL.
Total Grams
Grams.' dsct
Gr e.iTi= / ac f
Gr => i ns/'dscf
Grai n= /ac: f
Grams.dscm
G r a iTi s / a c ITI
Pouncis/d = c-f
Pounds /ac-f
Pounds/Hr
Ki1oqrams/Hr
. 10758OO
0072699
. OO43630
1121742
,0673985
2566995
, 1542347
O.OO0016O
O. OOOOO9i>
51 .25338OO
23.2483800
O.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
O.OOOUUUO
O.OOOOOOO
O.OOOOOOO
0.OOOOOOO
0.OOOOOOO
O.OOOOOOO
O.OOOOOOO
* BACK-HALF IMPINGER ANALYSIS WAS NOT REQUIRED
Proqr am Re •> \ si on : 1,
A-113
-------
APPENDIX A-2
PARTICIPATE MATTER CALCULATIONS
AND
ANDERSEN CASCADE IMPACTOR CALCULATIONS
-------
pi fiwr
Fi (-iNI K| IE
SMMFl.yUO L OCA !
i"F-:sr tt
DA T E
TEST PEPJi.it)
TIPHIO O> Si: — S
r:;.ftii rr.n JiL.rt T i:
FMO
POL-A i ELI.J ! „ li)Al!G
fNLET 2 -/
A -','
1 <) .'28 . 3o
0<-?SB- L234
is- Hsmpled st' =t:sndsrd c arid i I", i on=j (68 doq-F
,- :; V,r, :=.=• I I (Etr|) ^ 4oU"J :; I. Ph I- t Pffi' 1 5.. o I .I
P < 3l-.d) x i, I m H- 4oD>
1,,''i(i38 ••••: 12v»'VO8 '; 528 n I'. ,.:S , 68 i- < 2. •'
,,;,nn;- rd- = I- & n d ,i r d condj t-i onss
a n . i Iq ;
i i- l-ic.i :--ti.i-e. in
I 00
Vft. ( -;t-d '
I d. i
•|-_.i_t. |_r) ,-._.; (.jr.;
lid =
'J 'i q « 5 '
M ( q f\
H.O1. *
.1 '
A-115
-------
•s f^ ir-i if:r - a.... F: o ^ 8... n;::: n. ji n... <=» ~ r i c. n »-•
F;- ift o ife i - w o
.) rtv-f--r=i,-|e HoUjruljr W.--- i qh I ,~. !: HP,- stack g«= 3
Hkld -= < -44 - "..,[ i.J ,..'"> : < „ ^2 '••: ''•'.G2> i- (.28 •-' "M ,:- )
Mi-'id == '.,44 x ^;0'7I ; + (.32 •;•; 17.6 "> •*• ( „ 28 « 7A.o'::? ^ ~ 29., r> 1/6
) ' <:i • -Er-ri-iqe i'lrii (~r:i i i :~'" I- qas i:
i-iw =• MWd v fid i :!8< ! Md '
i'lH = '..."-'„ ^ I "ro M ,vl:'v1v'=;7 i-1£H! •• .V2v195'7 ) == 28. ^vc-/O2
i Stscl--' a -3= --'el C"~. i '' '•' in -}:e»t •-•pRi"-- m j ni.i'l" e (fprni flt sts»(~k cond i t-. i ons s
's - |--.J.-.>M;-|. v i bQP i 'dK> i : .b-..-f?': H '^i !R I i. i 3 l.^vq.: ! K 6QR I I" :l (PsxhW).! x oOse
1 '=: •= 8^,4^ v. , P4 -.; AO i: -:1::-,B '•.-174 >: SQPTi:i,'( :•:!=;. OQO 74 X 28.795O2 > .!
'.'= >; As y. Md ;••: T(std> x P<=
i i ._. ...i -... „
r ; \~ (.. i -— ..... " ....... ....... ....... ....... "
i 44 en j » i .. /c»u M' , x (-'\'~-
(Jsd = 7vc:;iI'2-OB dscfm
A-116
-------
s ^ MI F-- a EI 4 .. : - n'^ ii . . < ::;:
i~-> ^ n:^ E; : ~n ' a~ il IR: F--' ti .
« n •••• »
Ui !m-r<5 •; on* i ;.;onsi-^ni i; ™ |=: 4 '••:. oi.)
K4 = ,,Ov4K; FOR t !.|;i|. j ;;->H HiiT'lS
1 I ;•• 1-3 :; !1d - '. i On) -;:
, !~, /4 •-.; i O'.--, „ :,-!343 ;•: ""54 ,.
>: 14-J x •,:':•. .080 7 4 ;; . ^
( „ ..-.:-. 4 . "'.I L:i ";C.)2 < .
Efi == oo^.. J i
! ml .-i I- -j ; orio?ii'l r -?i !• i '"'i i s
Cs •=• ' . ii _MII-"-: nsr I .) ' '-'ni ' std ) ~
[';= == O , ' . i4i:rli:?Ci-'"\?ri Hr srns /i'jfjr i"
i • si d ' x I' Id •••• I'1*? ; i F
P'3t'd> r Ts-
a ~ • i „ ( i ,„• .1 4" :' 9 C'T.-*iTr= -'Br
.HS/HR = CE ;: • i= Od^:^:*.')^ x (Jsct x oU
B3/HP = •'.049VOA5X O.OO22?.t
HS-'IIP = ,'-. ..: ^.11^.4 o
A-117
Pfoqram Revi si.on ; 1 .
-------
Ft f* D 3: f^\\ "4 13 OII. I Ft O IE:. "T E.: S3 T'
IE! F:" ,Ph 1-1 El T" HI O O ::•> —- 5
O ^ r-1 IF" 8..... IE! O irt 8..... CI J S f* 8 I. O Ifvll
PI...ANT
PI ANT SITE
SAMPLING LOCA'I ION
TEST #
DA PE
TEST PERIOD
FMC
PUCATEU .O , IDAHO
IN I. ..El 2-1
B- 1.
10/27/83
14O1--1. /!53
iTie of dr>- qas sampled at standard cond i t i on= (68 deq -F i2'^',,':?2 in. Hq i
Y x '-,'m :•; i:r(std) -i- 46o:i x i:pb +(p«i/i3.ft) i
I I __ / „ 4- _J % —
*•' HI • ™->_'. .1 ' — ~ " " ~ ""
P'std) x (Tm +• 460)
.'^vv x ;| 1O,, J 76 -••: 528 >: C. 25.76 + •< 1,64 /13.ft)]
I i ._/_.. .L _i -,_. ___„_„ _ . „ _
- Hi - 1^> I *.( / — " " ~ ' .....
2",,':?2 x ( 1 OO.S + 460')
'>••'ui '' S'fc d I :~ 8'-? ., >.S 3yd Si" -r
me of i^ater ^ar/ior at. standard concli t :i':>ns s
3) P^i c.Riit ho.i -=t(.ii"cr in stack qas ;
'J - h/| .._. , __ _ ._.,
Vrn (=~l-.d ) •<- '.'wujas)
.1 (>(') ;; 3. '"^'32
Sc?.638 + 3.932
4) Mole fraction o-f drv stack gas :
tOO •••- "f'.M 10<'i -- 4., VO
McJ == — " "" ~ " " " " := •• 7 -•'' '''-•''••'-"'
1 nO ! ' 'O
A-118
-------
-1.. E O •ft 8.... C U L._ £* T I 01-4
TWO
rV, eraqe Molecular Weiqht of DRv stack qas :
f*|UJd - (.44 :• "/.CO2) i (.32 x "/.O2'> •'- < . 28 x %N.;.:>
hWd = (.44 -; 3.55 ) + C . 32 x 15.84 ) i- (.,28 x 75.61 > = 3O.OO1&
mveraqe Mo.lecu.]ar Weiqht of wet. stack gets ':
MW = MWd ;, Md •«•• 13(1 -- Mdi
MW = 3O.O01(3 x ,9579829 <- 18 U. - .9579829 ) == 29B49/:"5
Stack qas velocity in f set--per-mi nil he (tpm) at stack conditions :
: - r.'|.-i;=i',p x rSQRV u::i F' > .1 f a .- ^': x SURT FTs La^q;:! x SQR'I C 1 / (P<=xMW.> :i x 6Osec/min
'-'== •••-- 35,49 x .34 •-'.. 6O x 25.3938 .; SQRTi:i/( 25.17:1.77 X 29.49733 > 1
V:5 := 409!=, r '2.:':•'-. \'-P\-\
,..,., .-raqe -stack qas dry - r,.| ufius-t r i r: f 1 o«~i rate (DSt..;FI'l> s
Vs '- MS x I1d x Ustd) x Rs
144 cu „ i n „/cu „ f t „ y .,;/„ jo x 29.92
Hs.-i - 58598.01 dscFrn
A-119
-------
s #=* M F-- s... IE: G *=» ii c: L.j 5..... ^ T i: o KB
F-- *^» o IF; r i-1 F< HIE: FZ
1 =:Oki neM. c -sampling rate '•"'. > :
i.'i men si on a] Constant C - K4 x oO x 144 x I" 1 . (Pi / 4.) J
K4 ---- . 094!=r. FOR ENGLISH UNITS
C X Um(Etd) X HE 4 46O>
V=. x rt ;. PB K Md ••:-.. U')n'•••-2
10 3 9 . 5 7 4 x 89.63776 x ;|. O 27-16
4O95.. 223 x 144 x 25,. J.7377 x . 95'7982cii x ( .25 )-"2
) < Ex'~e=v=; air <"/. / s
I uO ..-: ";O2 1 OO x I 5. 84
til—( "= "" "" "" " ~~ '"" ' ""
(.264 x "/.hi.-: i - 7.O2 < . ^64 x 75.63 ) -• 1.5.84
EM = 384.37
i ci i] late Cane en tr «t i on :
('•<=, -• ' qrams part.) / Vm<=td> •= . 44O91 / 89.63776
Cs = O.OO491S8 Brams/DSCF
I ';=-td) x l"ld x PE x Cs
pfstcl) x Ti=
528 x .9579829 x 25,17377 x o., C».i491.88
2<:?. 92 x 1027. 16
r,a = <').OO2037£D Grams/ACF'
I.DS/HR = Cs x O.OO22O5 x Q = cl :•; 6O
LBB/HR - 0.0049188X O.O022O5 x 58598.O x 6O
I.BS/HR = 38. 1 33O6
A-120
r am Rev i s i on : 1 / :l 6 • &•
-------
s o»...« FC «"j: r~~ ~r i~:. s 'i
BE: IF- D=» 8 -11 E£! "1'" IH < I» D JS - '5
S rf=% 8"! IF- 8._.. EE. O iP» i C (. 88.. ,A, II' 1 O IN!
Pi «NT s FMC
PI .P.N I S U F 5 l-'i'tCAl EL I..O „ [Df-ii-lL'
9HMPLTNG LOCATION s iJUTLEl '2 -2
rEtn tt 5 c-i
DATE ". 10-'26/B3
TEST PEP I Of.) s o83'^-l 0^-7
of drv qas sampled at standard conditions ''68 deg-F
V :•-: '-'fit x 1.1 (Etd'i i doOJ ;; TPb H < Pm ' J 3 „ o .> 'J
I ,._ / __ 4.. -4 \ —-. _ _ _ —
' fll •!::-*„(_] .) — • " - "
P (i=td> :=• ( I'm --1- 4oO >
I ._ / --- L. ,_l \ _ _ „ _ .
'"111 \ '.~ < *...! ' - "" " ' " ....... "" ..... " ..... "
:::l-f-.^2 -•; '• 44.5!"i -i 460)
Vn|iiine of wat .. O4 7 1 '.-i •-. -f -• q rfi >; WQ> qm
yw(qas) = (").'.'.) 4 71'". ;: :l?7.2'..)-7 = 8.35'5 sr f
|-v?i-r-,?n I- |-|Q i =;i urs? jn stack qa= ;
! OO >-• Vw ', qas 1
" 1. 1 .._ _. __ _. ,_ .......... _ ..... ___ _ ____ _
Vrn ( ;; t d > <- V w ' q as )
49. O82 <- 8, :',SS
I'lol e traction o-f dry stark qas :
] <">O •- V.M K-M'I - 1.4.55
i i CI — — - ..... .— — . — . . -------
I'..!'1 1 OO
A-121
-------
13 /AI-1 9 F-~- 8 Er O t-^ I CI J! l._... ft "T" X O IMI
IF- »=* IPS IE: i" u* o
> fi- er=..:vs Molecular Weight of DRY stack qas :
!-1Wd = (,44 x ''.CO':: i i- (.32 ;••; ".'n(.)2 ' + •• . 2R x ".N2>
HW,-! == (.44 -; c=i.44 i -i- (.32 ••; 1 7. 7 ') ^ (.28 x 76.86 ) - ;'''V,,S784
)Averaqe Hoi (-?c:' .<:i ar Wei qhh oi: wet stack qas 5
MW == MUd x lvld •<- 1 B <1 - Mci >
MU! " 2^. ^784 n . 8 i=i 4 f« "> 4 3 ^ 18(1 - .8545343 ') = .?". 8^41 4
) Stack qa!=- veli~icity in f eert-per--mi ni.'t 'i :',.,. *••• i !; sUR'l I" '! s G-ivq )• :i >! SQFH" C :l / ( Ps;; MW > 1 ••; 6Ose
'-'== ==: 85.4V •>; .84 x AO ;.- 22,4434 x SQFTI: 1 / ( 25.78088 X 27,. 8'-?-U.4 >]
V=;. = .;,o06.83J I-PM
i a...-er ^QFJ stack c|.j= dry volumetric f .1 ow rate (DSCFM> s
'•..'•: ('Is -+-4ACI) x P(std)
:r.AO..S., 83 i x 47,,92
n = d •-- 775O0.45 dsc-fm
A-122
-------
-iiF-~"n ...EH. OV-ML. oil_JL._,rt 'i .11 OHM
E: r 1-1 R: JE: EV.
Iscski ne"1' :i c sampling rate ('•'. i s
i! i men si on ,-:-.! Constant- C .- | <-| ; .-><;> x i 44 x I. :l (Pi •'4) 1
1-4 ---. . Oc?4!=i FOR ENGLISH UNITS
i."; "••; Vm <-~1-.d > x C 1 .-. H 4o<.))
I. O 3c?. !=:i '7 4 x 4 '•? . O t? 1 •? 4 w 6 0 1 .. 9 3 8
3 '"'n :" " " ~" ~ " " " " '" "~
-'=s ^i r •":,.) s
•| (K.) x "CO",.' 1 i Hi x 1 ^y,, /
frV. = —- = - - -
'. . :,:\:>4 I.' V.N2) "-.U2 l.iO4 :! ~A.O6 ) I. 7 .. "7
EA = 63::;. 1.2
• i ci i] »\-<= Crincentr & I :i on :
Cs ~ < <:\r tnt'iB part. ) •' '-HI (=t- cj i — . \l:i,7,-i7 / 4'.1 „'.'ii:i J'V4
O. OO32 I 24 Orarns • \>'~>\. t
! (sl-d. x I-Id ".-. \-'~
P(std) x
C? - O.'M)2(.r'48 n,--,,n;= Ht F
I.BS--'HR - I";E jf O.O<)22Of> K (jsd :• oO
I. B':5/|-|R = O.0032124x O.(K>22Ofi x 7750O.4 x 60
LDS/HR = 32.^3756
A-123
Pr oqr am Rev i si on s 1 / :l. 6/ 84
-------
R'if-'-> D 1 iftM SOU IF-cr'^E:'
EE F> ,ft IMI E:: "ii if- • •« « ".ii i :> ::z: • s
is «=» K-1 F~-»... IL- ii: r * ~-•» ii _. r;« B it „ .ft
P! AN I" ;: FMi
PI AMI i:;riF. •: PI.H::MIELI..o
ShihPL 1 N(0 LGCMT I On s i i! I i |. ET 1 I
TEST # : I- - 1
DA rf; ;: 1 i / I./B3
i'EST PFP I 00 ; ij'r1'-,.?; - ! •..••-.!=:;
i .. / - - j — i ,
* in i ;.~ '. '.4 '
= ='Hip I f-d .-ii- <= i".snd.irri condi-I-i ons :; ' I in -I- 4c-M )
9 •-;•• 4 7 ;; 5B;, -..^4 v s .;•::< x r 25,,. bo -i- < .'73 /1"', & > "J
i/ij. <'-i|- ,-. 1-
0,,»47r"<
'.i, O47 'I !"-!
,' •• i^i ..^
'..,'n'. ( := 1" d ) "I- 'v'l'J '.. q S !r '
4'-"' „ 24fv + 11.
-'^c1!" i on of dry stscl
I OO -- "',,M
-- ....... --------------
1 ()O
1 v,
Md
A-124
-------
TWO
,.,-..,- ersq.~' Mo'l ecu I ar Weiqhl of DRV stsc!-: qas s
i'iw, I = t , 44 •;.; :UL:IJ,-:) -i- i . 32 :.; "/.ri,'.> •+ < » 2&
|- 1 l..j,:j = C.44 :; 8,73 ) t- (.32 >; :|.-b.O"r ) +
s) H^'STciqe Molecular Wei qht. ot i.jet. stack qss s
MU =.- |-| Wd ;: Md •<- 18 <1 -- Md'i
h!W ~ ,::•"•• . (?(S '."%<> M .SOA63J8 t- |Q(J •• „
7) St^i'k qs'-j '^eJ o-"i !: ••' in t- eel" -per— mi nut e !fi.,J8x '2'5, .''(.> .'3
) 1 '.; oOsec/min
dscfm
A-125
-------
" s. ... ie: Oipnii. d.J! .« T i o
T" MI F-< s~: E::
'-''') J soki nel" i c samplinq rate ',"•'./ s
DJ men-si ana I r.onstant C ••- I-:. 4 x 6i> -•: :l 44 x LI. / (p:i / 4.) :i
|:-.4 .•= . Ov45 FOR ENGLISH UNITS
C- ;i '--'IH '. = l"d ) :•! '. TB -i- 4oO )
T "/ __ _ __
V's ;- T't- •:. pa. K Md « (On1- "2
.IO39.574 ;; 4^ .24547 x 6O2.U3
3v''v8,4c>A x '•-,'•--,• x 2C;.7O7B ;; ,8066318 >; < . 183 ' -'-2
1";, = 1 1 2, --uw4
i O - fr;;i::es;; ;•. i i- <•"'-,'> ;;
1 I',11 ) :; "if 1'2 1. !")'.) ;; ] .':) „ O 7
( „ 2"4 "•••: ",,M2) - "v,O2 ' . Z'64 x 75,, 65 } - 16.07
E^A == 4 3. 1 „ 88
I s ) F'ir'r'M c 11J a t~e ConrC'ri l~r at. i on :
C=; = i ni-'anis part.) •' Vm(std) = .53134O1 / 49,,24547
C;= " ''>,, 01O38315 Gram=i/DSCI:;
T'"=t-d) x Ncl x Ps M C~
P
-------
FR f^ D T .ft T-.JI s < :» t.. J F< c: Er T e. s " r
ET IF" rt S -1 IE: "F H O O :3 S
r- it.... IET «::; #-1.«._.«.::«..»i .. .^" r i o fi M
FI-U::.
pi. .11 ,A I E.I Ml,. J i>M|-!i":.i
OUTLEI J - 2
I. -1
10.'31 .-:.!3
PL.AI--J r
PI r-.!-i i s n t
SAMPLING I. i.irA
TEST #
HA n-:
TEST PERIOD
1') './'nl niiie- o*- drv qs5; ESiTip J. eel uj-i- standard cond'J t i ori~. ' 4>B deq -F .. '
i x "HI x LT's-td) ^ 46O3 x LPb i-(.Pm •'13. b) !l
P f r=.-i-.d> ;; (. rm < 460)
?'-? „ '-''2 in. i Iq ')
'v'fiv,-t-d) :== 34. 6l"dS'-f
') '--'o I. t.i i n« of i-idfen -vapor -?.> h 'sl'.^ndard condi'l tonss
'w..'w iq->=H ) == '-.'•. '-.'A-''' 1 t;j e: f-. qrci ;; W<] .' qro
') Pe/i'.::onl- M.-.J -:• tur r:- in •.-:-. I ^..-.-k q.r.s ;
34 . oiO + 8. 'V'
-f f- 3 c t i on a f d r y st. & r. I-.- q
1 <")O ":.h
Md =
. 79405!:'i9
A-127
-------
^ 8-1 IF" I El. C.; .ft L. € 'I D III. .. irt ~T ' 1 O!! "
F'"ift, iBS1:- T' WO
; j Mv.-i=r-?qe Mol .-cu 1 -r Ul,--i gh !•; of DK'Y = 1: sck qa = ;
|-1 Wc1 := >: :, 4--I ; "iL"iJ2> -i (,52 \ ?/.GI"! H- (,,.28 v. ''-;N
•rlWd .-.- (.44 >; •".;.• ) < /. . 32 :•; I 6. S3 > + (.28 x
• ' \~>. - f=r i="7je I'lol ecu.! -jir Wft.i qh* o !• Net E'lrsck qas s
MW = lv)Wd ;: Me! -i-- IS', 1 - Md >
MIJ :== JS-.828 •; r 7v-4!)c:.S9 H- 3 8 ( ] •• , .: •?40'.~)B
") ':5t.?c!--: qs= v t;] oc i. •:••• sn I,-.=K-I- --per —mi ni.it r- (fpiu'i -j t Ki'y
condition;;
-'= - Kp: i..;p ; i 8i >PI ' dF1 > .! -i
8DPT r l"s ;.=-.v,-i; .1 H SQPI r 1 / '- Pssd-IW > 'I x 6Osec .'in.
) J
2'V2i ,. 21 •'•- l-r-'M
sl-d) >: P =
? '^ J.' I , 2 1 >:•! ;-, 4242.°2 ? x . 794O58v wri,.'.'B
Use! = 5:1"/7'2 . ^/' dscfffi
A-128
-------
s f^ir-i f-'- n IE;, rjrta...«
F" f^ Hi IE " I" II- « F."1=1. F:
iii men = i ona.! Gon=:t ynt I.. =:- l-~. 4 x >:-.•'> x 144 x i. ' •
I-.4 :.=: nov'r". l:i."iP IH-iQL fSH UNITS
I ' : '.'ill < i=t d ' '! ( 1 S i' 4oU )
]. ''- -'-• " " " " ...... ~" ' "
• 's =• I i- :: !-'=;. - M.-J x ,-iij. , 2
I 07.':? , l=; 74 x -":4 , 6 .!. d I 4 ;; 5'T.b -, 7-I
v:v.;'i , 2 i S3 ;; 9,b -.; :••!-,.':.•-;• 77 v :; , ~'^4O'5S^ •-( (
1 "„ = 1 03, .I :3oj
1 ;.K.I x 1 o. 8 '
. . _ _ ._
;^ (. .•,..•,->..( : T
'-Pi •' 4 > I
FA ~ =-21. .2.'.
,-i ij ,.:, \- f.. r ,-,nr i.-r. !-i- ,-,,-t- i OP
.- J O ! 4
'.-i 2 8
H-iS-'HF = r.:=, x t.)0 oo-,.::;.: os x Uscl x 6O
L .8 9 .' H P •- O . '. > 0 3 7 "' 8 4';; 0 „ O O 2 2 O 5
LBS/HP •= 25.8800,-,
A-129
Pr'ograrn Revisions 1 / lo, 84
-------
SASS DATA HANDLING
1. The results of each SASS run are calculated using the same program
as used for an EPA Method 5 run. However, concentrations and mass
rates are determined separately for the following particulate size
ranges: 10 microns and larger, 3 microns to 10 microns, 1 micron
to 3 microns, and 1 micron and smaller, rather than just the total
concentration and mass rate as determined by the normal EPA Method 5.
2. The mass emission rates for particulate matter smaller than
10 microns, 3 microns and 1 micron are determined by the following
formulas:
Mass emission rate in pounds per hour
>10 u = PR + IOC
<10 u = 3C + 1C + F
<3 u = 1C + F
<1 u = F
Total = PR + IOC + 3C + 1C + F
where
PR = Probe rinse as a calculated mass emission rate (Ib/hr).
IOC = 10-micron cyclone as a calculated mass emission
rate (Ib/hr).
3C = 3-micron cyclone as a calculated mass emission
rate (Ib/hr).
1C = 1-micron cyclone as a calculated mass emission
rate (Ib/hr).
F = Filter as a calculated mass emission rate (Ib/hr).
3. The flow rate through the SASS cyclones is calculated as:
V_ x
Qc = *"
c
A-130
-------
where
Q = Volumetric flow rate through the cyclones (ACFM).
V = Dry gas meter volume (DACF).
T = Absolute average cyclone temperature (°R).
T = Absolute average meter temperature (°R).
T. = Length of test (minutes).
P = Cyclone pressure (assumed to be equal to the stack
pressure) (absolute in. Hg).
P = Meter pressure (absolute in. Hg).
% M = Percent moisture in the stack gas by volume.
A-131
-------
ANDERSEN IMPACTOR PRETEST EQUATIONS
1. Calculate nozzle size from velocity traverse data and desired
impactor volumetric flowrate.
3.
Dideal = 2
144 Qn ,
[-w-^T1]'
2. Select actual nozzle size (D ) closest to ideal
3. Calculate orifice pressure drop.
AH = [846.72 Dn4 AH@ C 2 (1 - Bws)2
p=
] AP
s s m
Calculate impactor flowrate for AH and actual D. . -,.
V.9244 AH@
TmAH
4. If flowrate is unacceptable then go back to #2.
5. Definitions, where
. = Area of nozzle (F2).
Q = Volumetric flow rate through sampling nozzle (F3).
Q = Volumetric flow rate through dry gas meter.
m
D. . , = Ideal nozzle diameter (in.).
ideal
D = Diameter of nozzle (in.).
n
A-132
-------
Vg = Stack gas velocity (FPM).
C = S-type pi tot coefficient (0.84).
AH@ = Sampling train flow rate orifice calibration value for
0.5 CFM.
B = Moisture fraction.
ws
AH = Orifice flow meter differential pressure.
M . = Mole fraction of dry stack gas.
MW, = Molecular weight of stack gas (dry basis).
M = Molecular weight of stack gas (wet).
T = Absolute meter temperature (°R).
m
T = Absolute stack temperature (°R).
T. = Length of sampling period (minutes).
P = Absolute meter pressure.
P = Absolute stack pressure.
% M = Percentage moisture by volume.
A-133
-------
ANDERSEN IMPACTOR DATA HANDLING
Impactor Flow Rate:
n —
4n
V x £) x £)
vm (TB) (PS)
Tt
Cyclone precutter cutpoint is obtained from the manufacturers
calibration graphs of cut-point vj> impactor flowrate (Q ) and
applying a temperature correction factor.
All particle size data then is calculated by the PADRE computer
program using raw test data and the results of equations #1 and #2
as program inputs.
A-U4
-------
APPENDIX A-3
PADRE ENTRY FORMS
• RUNDATA
AND
• FILTER WEIGHTS
-------
Contractor ID. CNRTR: TR.v> Site in. SITE:_TF£X_ Test Date, IDATE:
Test Comments. TCOMH Ca\c<»*r ir-2. • ^VvC- Ro.1el)a ~dc,Kn-
Assumed particle density. RHO
Run index. [RUN (assigned)
Run comments. RCOMM
Run date, JOATE
Start time. ISTART
Duration, OUR (min)
Run type, RTYPE
I H20 1n stack gas
Composition of dry stack gas
'. CO?
I CO
1 N2
t 02
Ambient pressure, PAHBNT (1n. Hg)
Stack P wit ambnt, DPSTK (1n. HjO)
Stack temperature, TSTACK (*F)
Stack gas velocity, VSTACK (ft/s)
Impactor temperature, TIMP (»F)
Flow rate determination metnod
if EPA metnod 5, tnen
initial gas vol.. GMVOLI (ft3)
final gas vol.. GHVOLF (ft3)
volume water collected, VOLHjO (ml)
temp, of meter, TMETER (*F)
meter calibration factor CMETER
orifice iP. DPORIF (1n.
,
1 impactor flow rate, FLOW (ft3/m1n)
Max. particle d1a., WAX (microns)
Cyclone cut point, CYCL (microns)
Nozzle diameter, ONOZZ (In.)
Nozzle cut point, CUTNOZ (microns)
Was backup filter used? BF
Large particles on filter? FLARGE
Impactor type, IHPNAH
Impactor model , IHPHOO
Impactor plate set ID. I PL ATE
Number of stages used, NS (Do not
count cyclone or backup filter)
Substrates ID, IOSUBS (assigned)
(40
PADRE data entry font: run data.
v/
A-136
-------
PADRE ENTRY FORM
Location
Impactor
Run •
Date
Time
Substrates 10 (assigned) ">C
Descriptlon tr^ —rt
No. of weights
fi-2-l
Pre-Impactor 1.
Stage 0
Stage 1
Stage 2
Stage 3
Stage 4
Stage 5
Stage 6
Stage 7
Filter
7.
10
Post-weight
Pre-Weight
Weight Gain
Post-Weight
Pr«-weight
Weight Gain
Post-Weight
Pre-Weight
Weight Gain
Post-Weight
Pre-We1ght
Weight Gain
Post-Weight
Pre-Weight
Weight Gain
Post-Weight
Pre-Weight
Weight Gain
Post-weight
Pre-Weight
Weight Gain
8. Post-Weight
Prt-Weight
Weight Gain
9. Post-Weight
Pre-Weight
Weight Gain
Post-Weight
Pre-Weight
Weight Gain
•i i 5 C r.
V" 5
tt.cl
iiu.n
H.cl
JJ*.
<-• j / y
1. H
Total Weight Gain "L *7 3 • Tj
."Mi
lo .
/D ,T
3. In
i* l-
\.\~\
i-r JO
5.T 1
Z.
7?
- 47 4 "7
5 t
1. ??
/// 4. C^
1 , f/
3/5.
Weight units • milligrams. Order largest particlfi u iwlliit particles, first stage to backup filter
/
A-137
-------
Contractor 10. CNBTS: T£u)
Test Comments, TCQMM
Site 10, StTE:R=NL,
^ W "2. ' Fftvc.
Test Date, IDATE:
Assumed particle density. RHO !..-£> g/ml
Run index, IRUN (assigned) 4.
Run comments, RC8MM iv-i
Run date. JOATE
Start tim«, ISTART
Duration, OUR (min)
Run type. RTYPE
S H^ in stack gas
Composition of dry stack gas
S C02
I CO
I N2
t 02
Ambient pressure, PAH8NT (in. Hg)
Stack P wit ambnt, OPSTK (in.
Stack temperature, TSTACK (*F)
Stack gas velocity, VSTACK (ft/s)
Impactar temperature, TIMP (»F)
(clo« rate determination metftod
if EPA metnod S, tnen
initial gas vol .7~5
'Jas backup filter used? BF y
Large particles on filter? FLARGE
Impactor type, IMPNAM cu*.
Impactor model, IMPMOO n\ ILL
Impactor plate set ID, IPLATE 0
Number of stages used, NS (Do not 9,
count cyclone or backup filter)
Substrates ID. I05U8S (assigned) ?>3i'S
^•^•^•••^^•M
icS"
PADRE data entry form: run data.
A-138
-------
PAORE ENTRY FORK
Location
Impactor *
Run >
Date
Time
Suostrates 10
Description
No . of weights
Pre- Impactor 1.
Stage 0 2.
Stage 1 3.
Stage 2 4.
Stage 3 5.
Stage 4 6.
Stage 5 7.
Stage 6 8.
Stage 7 9.
Filter 10.
f- - : - /J -.' 1 .-'••"• /'; - " -1.
(assigned) 5". y."-' f2i -f2-j ?~ 57'
^ r 5~ 4 3(jJ • t-(T5J itt-lirtj
j <=\ -r — ' TW«
:-"
Post-Height _ -f ~ .'•)' -,-TJ i;" "• .
Pre-Height K ;' // _S-^' ^ '- ^ ' ? -"• 57.- ?y
Height Gain ' T — — ' i ^'', ^ - '.-;.- c: j. 5; ^ iy
Post-Height r_ ' if '' - -» :. -1
Pre-Height ~~ *- ~i-i ^ ^ y ^ ^,^~ , _,^_ _ ^
Height Gain il.le "'.t^' S.I! ^.?3
Post-Height ^ 3 /' C1 2- - ' **:,_•>/
Pre-Height - v- . ;' a*'-;.l-~! -! i ' ^+ L?'.<..7-f
Height Gain 'Y ''^- •?'°"1- 3- ^7 4 f 6
Post-Height H H 3 i, ^ - - ' . ^?.(.Ji'
Pre-Height ""/ 1 '- ^/i Z- 3 ^'S-'*'* ~j 2.C 7 •/
Height Gain ?'.=? Jt . S^ Ji . T- 5 |O. 5V
Post-Height ^'j 3 5 - ' '• -1 ^ :'," -• _. • /
Pre-Hewht " 1 /J 3~T ^'3 i> Z u < 1 "„ V/t '^"
Height Gain ? : '.' 6.2.) 4 33 i> •-'9
Post-Height 7w'c;J •" -.-,-. :| ...
Pre-Height " ^ '* H LI 3 f -1'-' ''•'' ~I5- ff
Height Gain !'•>.'•'•- 4.^3 1 11- i3.?7
Post-Height _^/ Z® u ~!^ J '. ^ i ^1", -•
Pre-Height -t \ - ' ^-/^" 5^ 'J: ^ f' ! v/i' -yt.1
Height Gain i.^' V.S5 j > / ? Io.r'
Post-Height T'-S 31/ • . ' ' -> "^ J t! • •• -•
Pre-Height -J:T' C1.' ^/'/ 7^ -"l^b* 1zy5"3
Height Gain 3.5-' ~L-'jO }.~>7 '-.^7
Post-Height V 2 ^ / 1 • ... J - -f - ' "L1 -y ,'.>">
Pre-Height ^^.^? f I/. ?/ 4-X'4i. Vtc'-?/
Height Gain /,a3 ' , ^ 1 . * V l.?^
Post-Height -y V ^ J3 •'• . .'•. '• ^ . 1
Pre-Height V ' - 3 * ^-'c/' "rV •*-. > :- v'J ? ?
Height Gain T- • 63 5-}5 2-^V 5.
-------
Contractor 10. CHRTR: TEvJ Site in. SIT£:_2T«c Test Qate. IOATE:
Test Comments, TCQMM G^~ 1*1.i P>>C fWlelb
Assumed particle density. RHO_
Run index, IRUN (assigned)
Run comments, RCOMM
I-OQ
Run date. JOATE
Start time, ISTART
Duration. OUR (mm)
Run type. RTYPE
; HjO 1n stack gas
Composition of dry stack gas
;g!
58
Ambient pressure. PAMBNT (In. Hg)
Stack P wrt ambnt. OPSTK (1n. H^
Stack temperature. TSTACK ('F)
Stack gas velocity, VSTACK (ft/s)
Impactor temperature, TIMP (*F)
Flow rate determination method
if EPA method 5, then
initial gas vol.7~5rWOLI ...
final gas vol., GMVOLF (ft3)
volume water collected, VOLHjO
temp, of meter. TMETER (*F)
meter calibration factor CMETER
orifice AP, DPORIF (1n. HjO)
te!se
* impactor flow rate, FLOW (ft3/«1n)
Max. particle dia., DMAX (microns)
Cyclone cut point, CYCL (wicrons)
Nozzle diameter, DNOZZ (in.)
Nozzle cut point, CUTNOZ (nlcrons)
Was backup filter used? BF
Large particles on filter? FLARGE
Impactor type, IMPNAM
Impactor model, IMPMOD
Impactor plate set ID. IPLATE
Number of stages used, NS (Do not
count cyclone or backup filter)
Substrates ID, IOSUBS (assigned)
TttS
4^(o. rso
(ml)
PADRE data entry form: run data.
A-140
-------
PADRE ENTRY FORM
Location
Impactor *
Run «
Date
Time
Substrates 10 (assigned)
Description
No. of weights
Pre-!moactor 1.
Suge 0 2.
Stage 1 3.
Stage 2 4.
Stage 3 5.
Stage 4 6.
Stage 5 7.
Stage 6 8.
Stage 7 9.
Filter 10.
' C/'
~
Post-Weight -."^.5~y ^ 1 '. ? i-
Pre-Weight & ilj 11. J >, i , ; -••• -, v ^ „ " -J
Weight Gain A^. ^ L' '•/-': 5'X.3/t ~> 'J ' ^>
Post-Weight T '""'•'•) •" '*' L / - *• • .
Pre-Weight l^'-i "' / :-3 Y?<".7J ^ V i 2.
Weight Gain ", -^ 3 3c-f j/ f / 3- 5k
Post-Weight -^';. -J.'1"' ."'j . . ...'..
Pre-Weight V^'-j"^ Y/5 -T^ 5'.*" ^ '; '-li'l^t
Weight Gain 1 5 5 1. 1 f- -| 8 "/ 0.41-
Post-Weignt •^^'^-'f fC^J-
Pre-Weight "1^~-,l~l i - ' ?J f^ .'..'•* 'l .V vc
Weight Gain f.t"? l.iT fc./o 1 . i5
Post-Weight -r. ^ "< J fl.,(tl - ~ -f • , -i '-
Pre-weight "- ; . fv 7.'1 5 -"- -^, 5 2 V/ ^.^"fr
Weight Gain J.'"> 1--1I J? . •• y ] . •? 9
Post-Weight -* 1 ' , "> "t 3 (, Yt " '- • "•
Pre-Weight *;7--.4(t V;j ^ J Js". '-*/ 'V/i 7y
weight Gain H,/<> T- ^ 1 J? . i 7- 1 . 1 •'
Post-Weight f.^./C- u','^\ •' ' - '- - ~
Pre-Weight ^|D."/C-' *i ; L - 1 ^ "'?" •*/ TLJ, Vt
Weight Gain 1..34 ! . 6 1- I.Lc 0 • ^ -£-
Post-Weight f,<7^1'3 'r:t(. -5 -'-'.'. - '
Pre-Weight ^l^.Sl -^..-"f '^J*' ^^ t 2.^ • (e 1
Weight Gain 1-40 ^''1. I'l^ O.^t—
Post-Weight ^."5 73 -flL.i'i -'- "> ~> - --J
Pre-Weight 'iJ'^O'i- v// J .1 ^ - ' .f ^/ - 2.^
Weight Gain <3.1(/ O.56 O.^T O. • /
Post-Weiont V_r ^ T1. -V^s Vt* ; • • - ." - ~;
Pre-Weight ^Sl L^ ^ i1 - Z6 •?"',•. _V ^ 7,7 . 7-5
Welaht Gain 1..7/ I.To !_.(/ O.CcT,
Toul Height G*1n 1o.0\ 6-5.S5 t2^ S'.'Ji ^^^— ^'''T
Weight units • nilKgrims. Order largest particles to smallest particles; first stage to backup filter.
/ J
A-141
-------
Contractor ID, CTRTR: TRq Site 10, StTE:(=fi»t- Test Date, IDATE:
Test Comments, TCOMM CLAc.'*/. impactor flow rate, FLOW (ft3/n1n)
-^lax. particle d1a., OMAX (microns)
Cyclone cut point, CYCL (microns)
Nozzle diameter, DNOZZ (1n.)
Nozzle cut point, QJTNOZ (microns)
Was backup filter used? SF
Large particles on filter? FLARGE
Impactor type. IHPNAH
Impactor model , IMPMOD
Impactor plate set 10. IPLATE
Number of stages used, NS (Do not
count 'cyclone or backup filter)
Substrates ID, IOSUBS (assigned)
4Tt iQO
ft 04^
PADRE data entry form: run data.
A-142
-------
Intentionally Blank
143
-------
Contractor ID, CNRTR: Tg.yJ Site ID, SITE:
Test Comments, TCOHH
Assumed particle dens 1 ty,
Run index, IRUN (assigned)
Run comments, RCOHM
Run date, JOATE
Start time, ISTART
Duration, OUR (min)
Run type, RTYPE
1 H20 1n stack gas
Composition of dry stack gas
-. C02
i cn
I 02
Ambient pressure. PAHBNT (1n. Hg)
Stack P wrt ambnt, DPSTK (in.
Stack temperature. TSTACK (*F)
Stack gas velocity. VSTACK (ft/s)
Impactor temperature, TIMP (*F)
Flow rate determination method
if EPA method S, then
initial gas vol.7~5iVOLI ...
final gas vol.. GMVOLF (ft3)
volume water collected, VOLHjO (ml)
temp, of meter, TMETER (*F)
meter calibration factor CHETER
orifice AP, DPORIF (in. HjO)
j else
• impactor flow rate, FLOW (Ct3/m1n)
Max. particle dla.. OMAX (microns)
Cyclone cut point, CYCL (microns)
Nozzle diameter, ONOZZ (1n.)
Nozzle cut point, CUTNOZ (microns)
Uas backup filter used? BF
Large particles on filter? FLARGE
Impactor type, IMPNAH
Impactor model, IMPHOD
Impactor plate set 10, IPLATE
Number of stages used, NS (Do not
count cyclone or backup filter)
Substrates ID, IOSUBS (assigned)
PADRE data entry
Test Date. IOATE:_l£2£ff3
I-O
A-144
-------
PADRE ENTRY FORM
Location C
Dun 1
Qitt
T1«t
Substritt* ID
Description
Ho. of Mights
Prt-Inotctor 1.
Sugt 0 2.
Stigt 1 3.
Stigt 2 4.
SUgt 3 5.
SUgt 4 6.
Stigt 5 7.
Stigt 6 8.
Sugt 7 9.
FtHtr 10.
IOJ.UI*i icflllri
S'^k^TT1 ^^~
_J — _a_
Post-Might lT3.'7i'" ^1^.2^
Prt-M1ght A,\"^f>3 3")J.(jf
Mlaht Sain Q. fe<< 2.5'?'
Post-Might 'f'"'. 7i *i' *?'
Prt-Miant (^Mll 13 mi.fZ
Miant Gi1n 0-6tf o.J9
Post-MUht Y'3 7C i^O I m
Prt-Mlaht M 13 («0 uOo "i4
Mlaht Gain 0./<3 o.'Z-"
Post-Mlaht V/-?.^' Mls"'jil
Prt-M1aht 41^01 -4 \
-------
Contractor ID, CNRTR: TL^ Site 10, SITE: gR-\C_ Test Date, IDATE: &z&*
Test Comments, TCOMM CtAct"-^- ^ I C-A.-i-^ ^ 1- ;
Assumed particle density. RHO \Cj^ g/ml
Run index. IRUN (assigned) lX
Run comments. RCOMM
Run date. JOATE
Start time, ISTART
Duration, DUR (min)
Run type, RTYPE
i HjO 1n stack gas
Composition of dry stack gas
; co?
i co
5 N2
5 02
Ambient pressure. PAMBNT (1n. Hg)
Stack P wrt ambnt, DPSTK (In. HjO)
Stack temperature, TSTACK (*F)
Stack gas velocity, VSTACK (ft/s)
Impactor temperature, TIMP (*F)
Flow rate determination method
/ if EPA method 5, then
initial gas vol .7~5ivOLI (ft3)
final gas vol., GHVOLF (ft3)
volume water collected, VDLHjO (ml)
temp, of meter, TMETER (*F)
meter calibration factor CHETER
orifice AP, DPORIF (1n. HjO)
e_1se
/"impactor flow rate. FLOW (ft3/m1n)
Max. particle dia.. OMAX (microns)
Cyclone cut point, CYCL (microns)
Nozzle diameter. DNOZZ (In.)
Nozzle cut point, CUTNOZ (ailerons)
Was backup filter used? BF
Large particles on filter? FLARGE
Impactor type, IMPNAM
Impactor model. IMPHOD
Impactor plate set ID. IPLATE
Number of stages used, NS (Do not
count cyclone or backup filter)
Substrates ID, IDSUBS (assigned)
PADRE data entry form: run data.
A-146
-------
PADRE ENTRY FORM
Location
Inpactor »
Run *
Date
Tine
Substrates ID
Description
fw of weights
Pre-lmpactor 1.
Suge 0 2.
Suge 1 3.
Stage 2 4.
Stage 3 5.
Stage 4 6.
Stage 5 7.
Stage 6 8.
Stage 7 9.
Filter 10.
/- - '
,
(assigned) • - -
•4-2fe? "2/S 7
e,
Post-Height - "•• Z.-1 . i i
Pre-Height • - . -r- , — , .
Height Gain o. / 1_ ^ •< >. 1 u
Post-Height . •* - -f ~ 5 ^V'
Pre-He1ght • . . - , ••:.." -. , -" .c... ,'
Height Gain r,,f-^ £~.~ly /2-.(/5
Post-Height - . . — -iZ-l-i b
Pre-Height . =• ' • - - : . _ . -i ., , >
Height Gain C.59 C.'/ 0.5^
Post-Height • - ; , ^~^.c}-+
Pre-Height • . • <-• " • - , • - i
Height Gain _&, ". -' O.15 0-1.1
Post-Height - - .- 4 1 3 :> 4
Pre-Heignt - L, . - - • " ;- -
Height Gain 0 , ~.
Post-Weight • : ~, , - - -1^4 .~?O
Pre-Height -t T -, ,' . . - . -r.. / •-, -i ... • .
Height Gain 0, L; 0 £> , r'>- / • IV
Post-Height -"_-)- '. 45u.Li't
Pre-Helaht - ' J -. . -" : • " ' * i , :. ' i •
Height Gain p . 39 O,c5 /.f?
Post-Height J -( a -. ... 4-t4. 4J_
Pre-Height • " - - ; • ? ' ' •'.-•">
Height Gain O. /5 " ,C~ C ,'9.fZ,
Post-Heloht - - • ~ ; •- . 5"?! ~7l
Pre-Wetght J '' - - • 3
Height Gain (,£2- &-~b1- H .IS
Total Height Gain '•,'. ~> V 1 • ^ ~ lo I • s y
Height units * milligrams. Order largest particles to smallest particles, first stage to backup filter.
A-147
-------
Contractor ID, CNRTR:_TU/o_ SHe 10, SITE:FP^ Test Date, IDATE: ta
Test Comments, TCOMM
Assumed particle density. RHO |.c"g, g/al
Run Index, IRUN (assigned) I (g
Run comments, RCOMM _-__
_
Run date. JOATE
Start time, ISTART
Duration, OUR (mln)
Run type, RTYPE
I HgO 1n stack gas
Composition of dry stack gas
: co»
I CO
I N2
S02
Ambient pressure, PAHBNT (In. Hg)
Stack P Mrt ambnt, OPSTK (In. HjO)
Stack temperature, T5TACK (*F)
Stack gas velocity, VSTACK (ft/$)
Impactor temperature, TIMP (»F)
flo« rate determination method
1f EPA method 5, then
Initial gas vol.T^VOLI (ft3)
flnal gas vol., GHVOLF (ft3)
volume water collected, VOLHgO (ml)
temp, of meter, TMETER (*F)
meter calibration factor CMETER
Orifice 4P. DPORIF (1n. HjO)
/else
impactor flow rate, FLOW (ft3/«1n)
Max. particle d1a.. DMAX (microns)
Cyclone cut point. CYCL («1crons)
Nozzle diameter, ONOZZ (1n.)
Nozzle cut point. CUTNOZ (microns)
Was backup filter vised? BF
Large particles on filter? FLAftGE
Impactor type. IMPNAM
Impactor model. IMPMOO
Impactor plate set ID. IPLATE
Number of stages used, KS (Do not
count cyclone or backup filter)
Substrates ID, IOSU8S (assigned)
PADRE data entry font: run data.
A-14 8
-------
PAORE ENTRY FORM
Location
Impactor •
Run <
Date
Time
Substrates ID
Description
No of weights
Pre- Impactor 1.
Stage 0 2.
Stage 1 3.
Stage 2 4.
Stage 3 5.
Stage 4 6.
Stage 5 7.
Stage 6 B.
Stage 7 9.
Filter 10.
(assigned)
~ r-, -
~
Post-weight z-'-".3 ^
Pre-Height
Height Gain !-i.2.LL- "**"-.
Post-Weignt 44- •\~!—
Pre-Height —
Height Gain o • 5r-
Post-Height 4-M •%$
Pre-Weight - '., " '
Weignt Gain i- , :"
Post-weight 4$£.5"4-
Pre-Weight -, ^ ^
Height Gain S, 1 !
Post-Weight 4-O. Szx 503
Pre-Weight -> . '!
Height Gain & • ''•'-'
Post-Weight 4i3 ~7 'S
Pre-Weight - - ,
Height Gain O> C- 9
Post-Height Aid-. "5 M
Pre-Weignt -i i . "- .
Height Gain U ' 2
Post-Weight ^ ZM . 0 ^7 - - ;
Weight Gain 0.94
Post-Height 4l~? 71
Pre-Weight "'' , ' •
Height Gain }• ff'1—
Post-Height ~^ZC. "7O
Pre-Height •'
Height Gain ~t-5. (jj
Total Height Gain Sc,T~
Height units • milligrams. Order largest particles to smallest particles; first stage to backup filter.
A-149
-------
APPENDIX A-4
PADRE COMPUTER PRINTOUTS
-------
'• GA; VELOCITi 'FT'SEC^s
PTYPE" I ;7Ai> TEMPERATURE • DEG F.s
C02» 8.5 I1PACTOP TEMPERATURE •DEG F,:
.0 MAX. PARTICLE DIAM. •MICRONS1
75.6 CYCLONE CUT POINT .MICRON;.:
15.a NQZCLE DIAMETER 'INCHE;'!
7.5 NOZZLE CUT POINT 'MICRONS':
lES LAPSE PARTICLES ON FILTER"
BAcujp FILTER USED' BF
•MPACTOR TYPE: IMPNA«=ANDERSEN IMPACTOR FLOW
' ACFcn l
IMP. PLATE ;ET
NO. IMP. STAGES USED N;=
NO. JETS DIAM. CUMDP CALIB
264 .1638 .0000 .3050
264 .1253 .0000 .4030
264 .0*48 .0000 .4100
264 .075* .0000 .3850
264 .0533 .0000 .36?0
264 .0343 .1760 .3600
2>>4 .0254 .2*40 . 3is20
156 .0254 1.0000 .2740
IMPACTOR DP SCALING FACTOR
ITPATES IDs
;P»PFEVES ANliEL
•/.CLONE 43
;TAGE i
FILTER
ENTER 'i OP
3 . 46 0 MG
5.000
2.550
4.270
3.360
4.160
2.34U
1.400
.760
2.710 MS
DO VOU MICH TO MQDIFV i*«Y PIJN CONDITIONS'
N
'JMNT TO PETPIEVE rtNOTHEP PUN' ENTER ~i OP N
N
DO YOU MliH TO TD PEDUCE THE D»TH' ENTEP Y OP N
100.0
13.5
.122
NO
FLOU=
DflT* REDUCTION HMD ENTRY '.YSTEH H-'ii 83 13i5ii:05
FCP TEiT BY CONTRACTOR TRW . HT -SITE FFMC. ON DMTE 10i63j. PUN NO. li
G MT 140.3 '- OF I^OKINETIC R>»Te
•«MMT TO iEE PESULTi IJ.J1N6 CLMiilCW. 'STOKESi DEF. OF DIW1.? ENTER Y OP N
N
UHNT TO %EE RESULTS UilNS TH€ TGLD DEF. OF HERO. DIhiM.: ENTER f OR N
N
UMNT TO SEE RESULTS USINS MERCERS DEF. OF ftEPO. DIfiM.T ENTER '. OR N
PUN B-i-i
TOTAL TIH;; *.T
G
034-002 1.1736-001
R-ACF GR DNCF
S MASS CUM.
1.0763*002 2.
MG- ACM
MA ; ; 05 o
' MG ' TAi5e >
FOP STAGE
INTERVALS
101
32
72
56
4 "?
27
18
13
10
0 1
• 1
1 2
. 2
• o5
,.57
,~->^
.51
.62
,66
,68
.31
.40
'MICRONS'
13
12
11
7
4
2
1
.
.
.
.
.
.
.
.
.
ARE SIMILAR
M1TH
KRE
WITH
D50-
S1MILA
05 dm
P
33
48
03
V-
>7
'•id
41
?0
33
OP
12.
OP
11.
0.337+002
MG'DNCM
GEO. MEAN
•MICRONS'
3»». 7:3
13.00
11.74
?.03
n.drt
3.73
1.9*
1.13
.6*
. 37
INVERTED
48 OMITTED
INVERTED
03 OMITTED
DMA^» 1 00. 0
MICRON;
DM DLOGD DN-- DLCGD
. MG DNCMi
I . -.c * i i 02
5.43*1,102
1.3 3*002
7* . 4 0* 0 0 1
7.4*»001
6.42*001
3.01*001
2.78*001
1.24*001
3.43*001
7
4
^
£
^
;
7
3
7
1
NO DNCM
. 36*006
. 77*008
. lo*uuy
.44+008
-4i*0«8
.36*009
.31*009
.68*010
.21*010
.23*012
FROM INTERPOLATION
FROM INTERPOLATION
: 'VALUES AT DIAM. MAPkED MITH • ARE EXTRAPOLATED
10
14
17
23
4*
78
110
l JZ
,39
.4*
.18
,3*
.08
.?')
-O1?
jtii —
1
1
2
6
10
15
£.0
.
.
.
.
.
.
.
.
•>'*
00
23
50
00
00
00»
00*
*. 31*000
2.73*001
2.32*001
4.23*001
7.39*001
1.73*002
1. 94* 002
2.38+ 002
A-151
-------
TEMP EPATlJPE =
TQP TE1P.« TIMS.
.;;T THF D-,T~ FOP
0? 'I
TE;T
TE:T I^HI
:.C'iTSAi,TCF T
TCOMM* Fir,
I- . MT SITE FFMI;. an DHTE iu
=OUHTELLT IDAHO: CALCIMEPi
ii« ;i3M r,r,
PUN COMMENTS:
DATE OF PijN:
•.TAPT TIME:
=UN DUPATION •
'. CAPBON DIOMDEt
CMPBOM MONOXIDE:
V NITPQ.3EN:
JD*TE=»
I START.
. : DUP =
PTYPE"
CO-
0£=
PNQa i . IJIJIJ
PUN B-l-c
30.0 STAi>
I STACI*
PPEiiUPE 'IN Hi5>
£i; WPT MMBIENT • IM
j VELOCITY 'FT-iECis
upE • DES e • s
3.5 IMPACTOP TEMPERATURE • DEG F«:
VE:
'. UATEP VAPOR:
BACHjP FILTER U-iED-
-L3W PATE
IMPACTOP T'.PE:
IMPACTOP 10DEL: IMPMOD=MIH
IMP. PLATE SET ID:IPLATE=
^0. IMP. STA'3ES USED NS»
'|Q. JETS DIAM. CUI1DP CALI
io4 .1£53 .0000 .4030
£»4 . 0?4i3 .0000 .4100
£o4 .075? .0000 .3350
io4 .0533 .0000 . 36?0
io4 .0343 .1760 .3oOO
I5o .0£54 1.0000 .i740
r5 FACTOP
DHA. PAPTICLE DIAM.
CYCLQUE CUT POINT 'MICPONS;:
NOZZLE DIAMETEP 'INCHES;:
NOZZLE CUT POINT 'MICPOn;<:
LAPi3t PAPTICLE; ON FILTEP-
ANCD CALC
QP FLOU FATE 'ACFM>l
ID:
DE;CP«*£EVEi
C'tCLONE
SUB:
£.?10
2 'if Ij
l.o£0
1..537 FILTEP
IMPACTOP DP
DO .'OU iJISH TO MODIFY ANY PIJN CONDITION.-;; ENTEP Y OP
iJANT TO PETPIEVE ANOTHER PIJN" ENTEP Y OP N
N
00 YOU MISH TO TO REDUCE THE DATA' ENTEP ( OP N
.700
11. J
. 1 ••> ij
1 j ij. J u
i3E» NO
IIliUBS
P*PTir.UU*TE JlMTft PEDUCTION h(ND ENTPY iYiTEM 11 -Si 3-3 13:?iil05
DMTS FOP TE:T BV CONTP*;TQP TPU . *T :ITE FFMC, QN DATE luc-iss. PUN NO. 13
-.HWPLING fit U?.* \ OF I>OKINET1C PftTE
,j«NT TO ^EE PENULTS UilNfi CLRiilCftL 'STOKE.i'i DEF. OF Dlwrt." ENTEP Y OP N
•«-» LINEMP ItiTEPPOLflTION USED BETUEEN
JMNT TO SEE PEiULTi US INS THE TiJLD DEF. QC SEPO. DI«1.'.
M
»»• LINEAP INTEPPOL^TIOh UiED BETUEEN .iS4ij*au3
V.HMT TO ;EE PENULT; UIIMS HEPCEPS DEF. OF
ENTEP Y OP n
.oijf i5733
ENTEP < OP N
PUN B-l-£
TOTAL MA;; *».5o5£-oi;
*3P ACF
;TASE MASS
• Ml3^ • P.
'ViCLONE 45.71
1 't.'ifl
£ £ . £ 0
3 £.o7
4 £.?!
5 £.?!
o 1 .o£
7 1.1?
3 .36
FILTER £.70
•*• CUT POINTS FOP
MEASURED DATA
•*» CUT POINTS FOP
MEASURED DATA
INTERPOLATED TO ;TD.
>£ 1.1 £47
-001 1.0
iajr*00£ £.
GP-DNCF Mi3-A,;M
MAS; CUM. IAS;
115. DNCI> •
179.66
1 j.£l
3.60
10.44
11.37
11.37
6.33
4.65
£.1?
10.53
;TAl5ES
FOP STAiiE
STAi5ES
FOR STAiiE
INTERVAL;
.
W3- DNCM<
73. 7£
65.31
56. ?1
46.47
35.10
£3.72
17. 3Q
1£.74
10.35
0 1 ARE
. 1 UITH
1 i APE
. £ WITH
: 'VALUES
ll.£?
15.17
17.41
£3.?1
43.30
68.37
a*. =17
lit.?*
D50
•1ICPONS-'
11.3.3
IO.**
:'.7£
6.31
4.38
£.47
l.£4
.30
.46
SIHILAP OP
D5i)» 10.
S I n I L AP OP
D50« ?.
AT DIAM. M
.63
1.00
1.25
£.30
6.00
10.00
15.00*
£0.00*
5733*00£
H3 DNCM
>3EQ- MEAN
•1ICPONS«
34.5?
11.40
10. S4
7.?3
5.34
3.£?
1.75
1.00
,61
.33>
INVERTED
'?? OMITTED
INVERTED
7£ OMITTED
At-* ED WITH
D1A.»» 100.0
MICRONS
DM • DLO'3D DN - DLDi3D
• Mi5' DNCM^ ' MQ.- DNCn*
l.?3*00£ •=>. 03*006
4.l5»uu£ 5.33*0u3
1.61+00£ £.73*008
3.??*001 £.£7*008
6.61*001 3.30*003
4.57*001 £.4^*00?
£.13*001 7.53*00?
£.40*001 4.66*010
?. £8*000 7.?£*010
3.31*001 l.?l*01£
FROM INTERPOLATION
FROM INTERPOLATION
» ARE EXTRAPOLATED:"
1.02*001
£.40*001
1.61*001
3.47*001
3.12*001
1.31*00£
l.S7»00£
£.3?*ooa
A- 152
-------
»•* IMPHCTOP TEMP.. TtMP. ;
DO .'QU WISH TO Li'.T THE inT A =
DATA FOP TEST E. CCNTBAi-.TOP TC
TEST COMMENTS TC^MMX Fir.,
PARTICLE DENSITY i'5M-cr,t
NO.
PUN COMMENTS:
DATE OF PUN:
START TIME:
-Utl DURATION .MIN
-UN TYPES
CARBON DIOXIDE:
• c*&SON MONOXIDE
• NITRGSEN:
'. QXYSENS
•. WATER VAPOR:
i,Af>up FILTER USE
CLOW PATF DETERMINATIONS METHOD
INPACTDP TYPE!
IMPACTOP MODEL:
IMP. PLATE SET IDMPLATE
MG. IMP. STAGES USED NS
INLET 2-11 tun B-i-1
102433 AMBIENT PPES-SURE .'IN »3 •
1 |J"56 3T»> P&ESS WPT AMBIENT 'IN H
31.0 STAC. HA". »ELCCITY •FT.-SEi"..:
I STAC» T5MPFPATUPE • "iEG F.;
7.1 IMPACTOP TEMPERATURE ' DE'3 F,S
. u MAv. PARTICLE I/1 AM. 'MICRONS'
C.CLONE CUT POINT .MICPON;'-.
NOIZ'.E DIAMETER 'INCHES':
NOZZLE CUT POINT 'MICRONS':
LnPl3£ P»6TIlSLEl ON FILTEP;
nD CALC
IMPNAM»ANCiERSEN IMRACTQR FLOW RATE 'ACFM<:
IMPMQD=Mlll
SUBSTRATES ID:
DEiCR'REEVE'S ANSEL SUBSTRATE
JDATE»
ISTAFT=i
DuR»
RTYP6»
C02 =
: C0=
N2»
02«
H.^Qs
5.i
16. 7
7.5
0
25.76
-i. 'JO
* 0 . 5 0
5 0 7 . ij
521.5
I 0 0. 0
12.4
cuTNor— 100.00
FLAP'3E» NO
1. JETS
264
264
264
264
264
264
264
156
DIAM.
. 163'3
.1253
. 0948
.0759
. 05 3 3
. 0343
.0254
.0254
CUMDP
. 0 0 >) 0
. 0 u 0 0
.0000
. 0 0 0 0
* tJIJUO
.17iaO
.2940
1.00 0 0
CALIB
.305 0
. 4 u 3 0
.410 0
. 3:35 0
. So^iJ
. So 00
. 3620
.2740
IMPACTOR DP
FftCTOR
1.237
CYCLDNE
JTA«
ST*5E
STA.3E
STA.3E
>TA*3E
ST*3E
STA.3E
STA.3E
FILTER
1
£
3
4
5
6
-
3
53.
11.
4.
6.
3.
3.
£ f
1.
.
2.
340
010
370
700
360
o20
600
750
970
110
MIS
MS
no YOU WISH TO MODIFY ANY PUN CONDITIONS' ENTEP < OP N
N
WANT TO RETRIEVE ANOTHER =IJN; ENTER V QP N
N
DO YOU UliH TO TO BEDUllE THE DftTA- ENT«-P C OP N
PrtPTICULKTE DfiTft PEDUCTION >W«D ENTBY 3
D«TS POP TEST BY I:OMTP*;TOP TPW . «T SITE PF"C« DM DHTE
S HT luii.i) '. OF liOKINETIC. PATE
TO -;EE PESULT; uiiw; CLSii i CAL >STOKESI DEF. OF
*• LIMEf* IMTEPPOLriTIDM IJiEL BETUE6M
TO SEE PEiULTS iJilMG THE TGLD DEF. OF *EPO.
** LIMEfiP
TO ;EE S
yi. PUM no. 5
EMTEP Y OP n
uiED BETWEEN •
s HEPCEP- DEF. OF SEPO.
ENTEP '<• OP N
6.5194332
ENTER . OR N
INLET c-U PlJN B-J-1
TOTAL MASS 7.uii'
up-
STAiSE MASS
•Mi3'
CYCLONE 53.34
1 11.01
2 4.37
3 0.70
4 3.36
5 3.62
6 i.oO
7 1.73
3 . >7
=ILTEP 2.11
»*« CUT POINTS
MEASURED D
»»• CUT POINTS
MEASURED D
•** LINEAR INT
INTERPOLATED TO S
j-uuc- l.oo 1 9-001 1.62
ACF i»P DNCF MI3
MASS CUM. MASS
'tliS DNCM^ • Mi5 DNCM>
231.31 144.ro
43.75 105.22
19.33 35. 3o
io.o2 59.24
15.34 43.91
14.38 29.52
10.33 I*.!*
6.:>5 12.24
3.35 3.33
3.33
FOR STAGES 0 1 APE S
ATA FOR STA6E- 1 WITH
FOP STASES 1 2 ARE S
ATA FOP STAi3E« 2 WITH
EP°OLATION UiED BETWEEN
TO. INTERVALS: 'VALUES
9.66
15.33
13. SO
29.15
54.91
118.32
176.77
220.73
21+U02 3.3077+002
- ACM Mi3/ DNCM
D30 i3£0. MEAN
'MICRONS» 'MICPONSx
12.44 35.27
11.34. 11.33
10.02 10.66
6.71 3 . 2 0
4.51 5.50
2.35 3.39
1.23 1.31
.32 1.03
.43 .63
.34
I1ILAP OP INVERTED
D3'j« 11.34 OMITTED
IMILAR OR INVERTED
D30» 10.02 OMITTED
4.5144148 6.
AT D1A«. MARKED WITH
.63
1.00
1.23
2.50
o.OO
10.00
11. JO*
20.06»
DMA\= 100.0
MICRONS
DM-DLQi3D DN DLOI3D
• MI3-DNCM. .NO' DNCM
i. 56+002 1. 11+007
l.ij^+'jijj 1.24 + UU'-
3.61+002 5.70+008
1.53+002 5.29+003
3.91*001 1.02+009
5.73*001 2.33+OU9
3.47*001 1.12*utO
3.39*001 0.33*010
1.64*001 1.27+011
2.79*001 1.38*012
FROM INTERPOLATION
FROM INTERPOLATION
7103418
• APE EXTRAPOLATED.
1.63*001
3.60*001
3.11*001
4. 39*001
3.91*001
3.29*002
3.48*002
3.32*002
A-153
-------
TE1F., T|Mt, iHQij
IST TME DATA FDF
EE
DATA CQP TEST
TEST •-.:"^MT;
DENSIT
CQNTPACTQP TPU . AT SITE PPMC, QN DATE I0i633, ClJH '
CUN TYPE:
'. CAPBON DION IDE:
• CAPSCN MONOXIDE:
INLET 2-1S
IU2883 AMI
'IN
PTYPE* I
C0»
'. WATER VAPOP: H2Q
fcAcujp FILTEP U;ED; EF
PLDW PATE DETERMINATION:
IMPACTOP TYPE: IMPNAM*ANDEPSEN
STAC' TEMPEPATUPE • DEG Fit
7.t IMPACTQP TEMPEPATUPE •DEG F
.o MA%. PMPTICLE DIAM. 'MICPOM
76.2 CYCLONE CUT POINT 'MICRONS.
16.7 NOZZLE DIAMETEP 'INCHES;:
7.5 NOZZLE CUT POINT 'MICRONS^:
; LAPSE ^ARTICLES ON FILTER?
IMP. PLATE SET ID:IPLATE=
MO. IMP. STAGES USED NS=
NO. JETS DIAM. CunDP CALIB
264 . l n 33 . 0 ft 01) . i 05 0
i64 .125-3 .0000 .4030
264 .0^43 .0000 .4100
264 .0759 .0000 .3850
264 .0533 .OOuO .3690
264 .0342 .176U .3600
264 .0254 .2940 .3620
15« .0254 1.0000 .2740
IMPACTDP DP SCALING PSCTOP
PSiTE
DEiCP»PEEW6i ANSEL SUE^
CYCLDN6 70.230
. 62 0
1.150
1.410
STSI5E
1.287 FILTEP
DO YOU uISH TG MODIFY AMV PUN COhDITIDN-i: ENTEP Y DP N
.JANT TO PETPIEVE ANOTHEP PUN"? ENTEP Y OP N
N
.32o
.310
.630 MS
;T*:t<= 3*. an
'iTft:!'" 4'iJ.i)
TIMP. 5i0.rj
DMfiX« IQij.ij
C'('CL» 18. e
UTNOr
100.00
NO
PLQU»
DO YOU
TQ TO PEDUCE THE DftT«: ENTEP i QP N
PAPTICULATE DATft PEDUCTION AND ENTPV SYSTEM U 22 83 13:56:05
DATA POP TEST BY CDNTpMllTOP TPU . AT SITE FFMC, ON DATE 10268JI, PUN NO. 6
;AMPLINS AT 69.4 •. OF ISOKINETIC PMTE
•JMNT TO SEE PESULTS USINS CLAisi.SM. 'STon^ DEF. OF DIAM.. ENTER Y OP N
N
»•» LINEAP INTERPOLATION USED BETWEEN .51856852 1.0167698
»*• LINEAP INTERPOLATION USED BETWEEN 9.5'946186 18.600000
.JANT TO SEE RESULTS USINS THE TGLD DEF. QF A£PO. DIAH. 7 ENTEP Y DP N
•N
»»» LINEMP INTEPPGLftTION USED BETMEPN .5185b«55
«-»» LINEUP INTEPPOLliTION USED BETUEEN «.5?*61S6
UMNT TO iEE PEiULTi UilNij MEPCEPS DEF. DF M£PO. DIMM..
18.600000
ENTEP Y QP M
INLET 2-11 PUN B-2-2
THTAL MA;; i. 54*4-001 3.1101-001 3.0794+002 7
|JP ACF GP ' DNCF MS' ACM
STAGE MA;; MAS; CUM. MA;; D50
'MG» 'MS'DNCM> ' MS' DNCM1 -MlCPONS
--YCLONE
1
2
3
j
5
6
7
.5
FILTEP
«-»+
»-»»
70.23 613.42
3.56 31.07
.62 5.41
1.15 10.04
1.39 lo.50
1.41 12.31
.32 7.16
.32 7.16
.31 2.71
.68 5 . 94
CUT POINTS FOP STAGES 0
MEASURED DATA FOP STAGE,
CUT POINTS FOP STAGES 1
MEASURED DATA FOR STAGE,
98.28
67.21
61.30
51.76
35.26
22.99
15.30
3.64
5.=^
1 APE
1 IJITH
2 APE
2 MIT*
13.60
16.54
14.62
9.79
6.53
3.71
1.37
1.20
.70
SIMILftP DP
D50» 16
SIMILAR 0°
D50» 14
.1170+002
MG DNCM
DMAX= lOO.'J
MlCPONS
D50
13.60
16.54
14.62
9.79
6.53
3.71
1.37
1.20
.70
GED. MEAN
' 'MICRONS'
43.13
17.54
15.55
11.96
3.03
4.94
2.64
1.50
.91
.49
DM' DLOGD
' MG DNCM <
3.40+002
6.08+002
1 . 0 1 + o Uc
5.76+001
9.53*001
4.95+001
2.40+001
3.70+001
1.15+001
1.97+001
DN DLDGD
'NO- DNCM
2.00+007
2. 15+008
5.14+007
6.43+007
3.54+003
7.32+008
2.51+009
2.11+010
2.38+010
3.15+011
16.54 OMITTED
0» INVEPTED
14.62 OMITTED
LINEAP INTERPOLATION USED BETUEEN ,69702046 1.1
»•« LINEAR INTERPOLATION USED BETWEEN 9.7865798 13.
INTERPOLATED TO ST1. INTERVALS: 'VALUES AT DIA«. MARKED WITH
r.74
9.41
17.32
32.34
53-32
32.70
106.42
1.00
1.25
2.50
6.00
10.00
15.00
20.00*
FPOM INTERPOLATION
FROM INTERPOLATION
982656
OOOOO
• ARE EXTRAPOLATED*
1.15+001
3.25+001
2.19+001
9.79+001
1.48+002
1.67+002
3.46+0 02
A-154
-------
«»» IMF-AC TaP TEMP.. "j^'.'l ",HQULD BE
liO i3U HI Si TO LIST THE DATA FQP PUN' ?NT =
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anTP*-,Tnp TPU . *T -,!f- FFKH;. an &ATF lOi^iv- ~>JH -c. i-
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PAPT1CLE DENSITY "5H
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JDATE* 102-5-33 A
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14.13 NOZZLE ClIAfltTEP 'INCHED':
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ES LAPiJF PAPTICLEi ON FILTEP'
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N
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SUN 6-3-1
TOTAL MAIS
i.iie^-uui
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1
4. 33
372. 03
24.52
17 . 05
la.25
1-3.60
13.12
3.13
1.77
1.04
3.34
7.60
4.4?
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•*» CUT POINTS FOP STAGES
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MEASUPED DATA FOP -JTAi-JE.
INTEPPOLATED TO iTD. 1NTEPWALS:
3,££aa-i)i)l 1 ,8:33-r'»OrJc:
050
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12.03
11.21
0.64
4.4.J
2.52
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1.00
1.25
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6.00
10.00
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1 3»» . 62
112.10
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3:3.20
40.07
26.41
13.31
14.33
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34.6:3
11.•=!
10.54
3.11
5.44
3.35
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1.01
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INVEPTED
21 OMITTED
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DM-DLOGD DN- DLJSD
1113 DNCMx .MQ DNCMI
4.04»i)u2 I.:35*no7
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165.70
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4.33*001 1.33*010
3.-f)3*001 7.13*010
l.-j-rH-OOl 1.32*011
4.77*001 2.45*012
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3.'?il*001
3.77*001
5.70*001
1.32*002
2.46*002
3.63*002
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A-155
-------
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564 . 0554
156 .0554 1
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iT 107.3 '. QF UOKINETIC P*TE
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•»«» LINEftP INTEPPOLfiTION u»ED B6TUEEN 7.3336333 14.564400
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50.35 51.55
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1.13 5 . 33
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1 . 03 5.60
55.67 65.40
CUT POINTS FCP ;T*3Ei
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76,37
76.33
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75.03
73.33
70,40
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5nP«.-,TQP TE1PEPHTIJPE • DE'5 c
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IMP. PLATE SET IDSIPLATE-
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i64 .1638 .0000
264 .1233 .OOOo
264 . ij^4Ji .0000 ,4100
264 . 0731? .0000 .3850
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DATS FOP TEiT BY CONTpBHlTOP TPU . >iT SITE
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N
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'=•7.33
31.72
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133.76
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133.57
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131.16
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136.6*
133.37
153.33
173.43
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14. 14
1 !.•=•-
10.53
7. 08
4.76
2.6?
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030- 11.
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D50» 10.
4.76435
MG. DNCM MICRONS
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37.0'j
13.01
11.25
3. 60
5.31
3.53
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1.15+002
4. 33+ 302
2.72+ 301
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2.03+002
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3!o4+o07
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3.23+007
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0331 073
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7.47+000
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A-157
-------
;THISE
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IMP. PLHTE ;ET ID:IPL*TE
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564 .1553 .0000 .4030
564 . ll**3 .0000 .4100
S64 .075* .0000 .3350
564 .0533 .0000 .36*0
564 .0343 .1760 .3600
564 .055* .5?*0 .1650
156 .055* 1.0000 .5740
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13:56105
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LINEnP INTEPPOLHTIQN UiED BETUEEN
. .33833675
5.15613>»='
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• LINEHP INTEPPOLHTION USED BETWEEN
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.33335675
5.156136*
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7.710.3T60
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7.7103760
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1
5
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5.5035-001 6.0535-001
i5R H<;F SP-DNCF
5.73*5+005
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11.65
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6.03
4.01
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1.45
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06 . 5 0
30. *7
34.55
55.7?
17.10
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6.55
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14.64
13.35
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1.51
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•*» LINEHR INTEPPOLHTION U
INTERPOLATED TO STD. INTERWftL
:a55*003
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33.56
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=•.65
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5.13
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1.4j*0ij3
1.65*0ui
5.73+oui
l.*8*00e!
1.35+005
6.33+001
5.77*001
3.53*001
3.51*000
5.15*001
100.0
MICRON;
DN DLOi3D
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4.37+007
1. 15+00*
5. 5*+ oo3
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5.07+00'f
5.4*+00*
3.50+010
3. M + 010
0.54+011
1 HPE :iMILHP OP INVERTED
1 WITH D50« 13.35 OMITTED FROM INTEPPOLHTION
5 *PE ;IMILHP OR INVERTED
a WITH D50- 11.30 OMITTED FKQN INTEPPOLHTION
SED BETWEEN .56530*47 .*-»70007*
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;s .VHLUES HT DIHM. MHR>ED WITH » nRE EXTPnPQLHTED•
6.35
15.10
355.50
A-153
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jn
r:Q iQU
iFAc'.TUR TEMP.. 4-nj.u
.IS" TO LIST THE DAT-
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5 IS Hi3n
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TEST COMMENTS TCOMn= CMC, PQCATELLO IDAHO: CA^iSINEP
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PAPTICLE DENSITY . i
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DATE OF PUN:
START TIME!
PIJN DURATION .MINi
=-UN TYPE:
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' CARBON ir]NQ\IIiE:
PTYPE- I
AMBIENT PRESSURE 'IN -'3'
STAC" liAS VELOCITY .FT-SEC-:
INPsr.TOP TEMPEI
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BACHJP FILTER USED"
-LOU PATE
N:0?
D*T« FOP TEST BY CDNTP<4CTOP TPU . «T SITE FFWS. DM DflTE UJSo83« PUN NO. £
SanPLlNS HT -«i.r '.. OF liQKINETIC PATF
iu«NT TO SEE PEiULTS USIN5 CLM-ilSICftL 'iTOKES> DEF. OF DIM".' ENTEP Y OP N
•N
•*» LlNEl*P INTERPOLATION U-SED BETUEEN .£'8*4*0*7 .^08*50^5
'J«NT TO SEE PESULTS USINS THE Ti3LD DEF. OF S£PQ. DIftn.? ENTEP Y OP N
•N
«-*» LINEAR INTEPPOLftTION USED BETWEEN .ii^-iWr .iClB^*^
•OHNT TO SEE PEiULTS USING MEPCER'S DEF. OF HERO. Dlnn. • ENTEP Y OP N
INLET i-i»«JRUN H-\-S
TQTHL MftSi i.?ri5-tj')l
i5P «"SF
STSniE
MftiS
CYCLONE
1
2
3
4
3
o
7
3
402.32
17.03
3.4*
16.51
10.33
10.78
3. 13
3.10
1.27
1401.14
57-. 31
5-?. 3*
59.45
37.7*
37.5*
17.**
10.30
4.45
593.?*
5 0* . 93
175.23
113.33
31.0*
43.30
55.59
14.77
10.34
11.39
lO.o?
•?.45
9. 33
4.2e
2.40
1.21
.77
.45
34.00
11.12
10.05
7.74
5.1*
3.20
1.70
. ?7
. 5-7-
DMA'v» 100.0
' DNT.F 1i3'AlSM Ml5/DNCM MICRONS
CUM. MASS D50 i3ED. MEAN DM • DLOGD DN • DLOGD
• MI; DNCN» 'NO- DNCM<
1.30+003 7.57 + IJ07
1.73+003 5.44+00-?
5.4*+Oo2 1.03+00*
3.54+002 1.34+ijij-?
5.1*+005 i.OO+Oo*
1.51+002 3.32+00*
9.02+001 2.32+010
5.33+001 1.13+011
1.33+001 1.74+011
.32 3.44+001 5.04+015
1 APE SIMILAR OP INVERTED
1 WITH D50= 10.91? OMITTED FROM INTEPPOLATIOM
2 APE SIMILAR OR INVERTED
MEASURED DATA FOP STASE. 5 WITH &50» *.45 OMITTED FPQM INTERPOLATION
»*• LINEAR INTERPOLATION USED BETUEe'N .45003177 .7749412*
INTERPOLATED TO STD- INTERVALS: 'VALUES AT DIAn. MAR«ED WITH + APE EXTRAPOLATED!
13.05 .63 1.33+001
50.37 1.00 5.91+001
25.75 1.53 3.22+001
45.43 2.50 l.lii+002
lll.On 9.00 3.19+005
10.00 9.91 + 005*
13.00* 1.56+003
20.00* 1
=ILTER i.J7 10.3*
•*• CUT POINT-: FOP ;TI*SE> o
ME*-;UPEII DHTR FOP ST*;E.
«-•» COT POINT, FOP
A-159
-------
0!iL, Jp C
:ATE 3F =•!.,« s Jj-TE= 1 0£ b '-. i A"iil='i: =-=;;ij=E • I'i -t'3 •
•.TACT TIME: IiT«iT= 1007 ;TAi> =•£;; --T ftnfclFiiT .
= UN T.FEi PTVPEs I ;THI> •tEMtct.HT'.JPE .0000 .36-=tO >TCn»E 5 6.610
i64 . 0£5«J. .£940 .36£0 iTi^iE 7 1.110
156 .Oc54 l.utjOO .£740 ^TPM5E 3 .660
IMP»CTOP DP iCfttlNS F«CTOP l.£37 FILTEP 1.4£0
DO lOU uliK TO MODIFY .=tNY SUN CONDITION';: ENTEP v OP N
n
UMNT TG PETPIEVE i*f .lii
> lOu.'Ji.
;» 10
PftPTICULHTE BftTrt eellUCTIOh >»ND ENTP'l i'tiTEM 11 -££'8.3
inT« POP TEIT BY CQNTPW;TOI' TPU . AT ;ITE PFMC« ON D«TE ioa
;*MPLINi; AT li*.l ': OF I^GklNETlC PftTE
'jnMT TO i£E PEiULTi USING ilLftVilCflL 'iTQti DEF . OF DlM«.'
•«-» LlNEi*P INTEPPGLrtTION uiEL BETUEPN 1. ££,04iJ£
U«NT TO ;EE PENULT; UJIMS THE TGLD QEF. OF «EPO.
PUN NO.
ENTEP'
OP N
ENTEP v GPIN
«-«-» i.INErtP I
IUF*NT TO iEE PE'i
't'
INLET £-£! PUN
>3
' MlJ
•• .'CLONE £41.
1 li.
£ 5.
3 11.
4 5.
3 6.
? £.
7 1.
3
•ILTEP 1-
NTEPPOL&Ticn U.;ED BETWEEN i.££04o
ULTi U^INIJ MEPCEPI DEF. OF ftEPQ. DI
61i-u01 6.4317-001 6.3I35*00£ 1.
P-^H^F ijPxDNCF MI9--NCN
i nf>~,3 CUM. Mft'^i D50
' ' MlV JNI^M t
-i 1
41
0£
11
71
61
53
11
66
42
£6.3 . 1 0
53.60
££.4*
4C..7S
£3.53
£Cl.6d
11. >4
•*.'?"
£.*6
6. 36
*»• CUT POINTS FGP ;T*ses
MESSUPED
DATA
FQP iTft^E
*«-» CUT POiHTS F0» -.TWEi
nEH>UPED
••• L I N£MP I
1NTEPPOLBTED TQ
DATS
NTEPPO
iTD.
FOP -vTWE
LHTIQN u;
MI? DNCMI
i O'.i
153
130
30
53
J5
14
-i
6
0 1
. 1
1 £
. £
.>»:•
. O1-
.60
.33
.£4
.6.3
.£•?
. 3£
. Jn>
APE S
WITH
*PE ".
IJllM
ED BETUEEN
INTEPVSLis 'V»LUE;
7
10
13
c4
63
13s
£47
40£
. 06
.36
. U*
. r?
.50
. 1?
.37
.61
iMICPGNi.
13
1^:
10
7
,
.
.
.
4.
£
1
.
.
.
.
INIL*P
D50«
IHILl*
D50»
1.
P
3
13
14
73
19
33
73
37
3d
51
OP
1£.
OP
10.
7"i 16
*T D;*>«. M
1
1
£
,,
10
13
£0
f
,
f
.
„
,
,
-
63
00
£3
50
00
00
00*
00*
i£4 £_56*=- 135
ftfl. ' ENTEP V OP r4
4713*003 OMPlX" 100.0
Mij'DflCM MICPQN5
'3EO. MEAN DM DLQGD DN-DLO'SD
•MICPONJ'
36. 30
1£.65
1 l.4i
3.73
3.3-?
3.g3
1.^3
1.10
.67
.36
INVEPTED
14 OMITTED
INVEPTED
73 3MITTPD
13 £-
KPkED WITH
'M
1.
1.
4.
2.
1.
1.
3.
£.
1.
£.
'|J. DNCPi'
44*003
56*003
£0*0o£
36*uO£
4**06c!
l**uuS
31*001
57*001
£6*001
11*001
• NO [INCM .
5.73*007
1 . 47+l)IJ -
5.3'?*u03
3.05*003
1. 3^*00f
4.73+00*
1. 00*01 0
3. 70*01 0
7.?5»010
3.53+011
FPQM INTEPPOLMTIGN
FPQn INTEPPQLMTION
7£6
*
1.
i.
£.
4.
1.
3.
3.
1.
^*i-i«j
APE EXT
07*001
37+001
36*001
O'i*0ol
61»00£
05*0 u£
77»00£
55* 00 3
P»PQLHTED;
A-160
-------
WISH TQ _IST T~i D«T* erjf
C TEST EI c3NTc*r.Tj= TFW
T£ST COMMENTS
-"-SINEC ::l
-HPTICLE DENSITY
S-UN COMMENTS:
D«TE OF OIJNI
.THRT TIME:
RUN DUSnTlDM 90
. 3600
156 .0254 1.0000
IMPHCTQP DP SCALING CH
YOU 'JI>H TO MODIFY
CYCLONE
STHiJE 1
>T*'5E
3
.'ES RNGEL SUBSTRHTE
24-^,474 MG
li. 01 0
; 1.237 FILTER
PUN CONDITIONS' ENTER Y QP N
I . 7 1 0
1.44 0
2.040 MG
TO RETRIEVE HNQTHEP RIJN:
ENTER
0*
DO YOU UI1H TO TO REDUCE THE D*T*7 ENTER Y OR N
N
PftPTICULHTE DHTH REDUCTION HND ENTRY S.JTEM l:
DHTH FOP TEST BY CONTRACTOR TRW . HT SITF. FFMC. ON
1G HT 3S.4 •-. OF ISOKINETIC RHTF
TO SEE RESULTS USING CLHiSICHL 'STDI-ES* DEF. OF
••» LINEnP INTEPPQLHTION uiED BETWEEN 1.1095235
»» LINEnP INtERPOLHTION ulED BETWEEN 4.3c410-31
TC ;EE RESULTS uilNi5 THE TGLD DEF. OJT rt€PO. DlHfl.T
•*» LIMEfiR INTERPOLftTIDN UiED BETUEEN 1.1 0*5335
•*»LlNEftP INTE=POLhtTION USED BETWEEN 4.3i4103l
•JHNT TO SEE RESULTS USING MEPCERS DEF. QF H£RQ. DIHM..
PUN NO. 4
ENTER Y OP
ENTER Y OP N
i.3r>4'?;7l
ENTER Y OR N
STftSE
2.4133-401 5.471
GP-HI-
MftiS
• MG .
148.47
26.71
6.19
12.01
6.70
7.98
2.64
1.71
1.00
2.04
:F SR-
MHiS
'MG'DNCH)
986.37
106.09
24.59
47.70
26.61
31.70
10.49
6.79
3.?7
3.10
52-401 5.5340*442. \.i
• DNCF MG
CUM. MHSS
•MG.-DNCMl
266,03
15*. 94
1 35.36
37.66
•> 1 . 05
29.35
18.37
12.07
3.10
;529*04i
/ HCM MG' DNCM
D50
•MICRON-Jx
12.24
11.30
9.99
6.69
4.50
2.54
1.28
.32
.48
GEO. MEHN
'MICRONS*
34.9*
11.76
1 O.o3
3.13
5.49
3. 38
1.30
1.02
.62
.34
DMH*» 144.0
MICPONS
DMx DLOGD
•MG- DNCM>
1.43*003
3 . 06* 0 43
4.59*442
2.74*4u2
1.55*002
1.27+002
3.52*001
3.51*001
1.69*001
2.69*001
DN- DLOGD
'NQ^ DNCM
4.32*0u7
3.60*009
7. 31*408
9.57*008
1.79*04*
6.31*009
1.15*010
6.26*010
1.32*411
1.35*012
4
5
7
3
rILTEP
•*• CUT POINT'S FOR STHGES 0
MEASURED DHTH FOR STHGE.
.«« CUT POINTS FQP STHGES 1
MEHSUPED DHTH FOP STfiGEm
•«-• LINEAR INTERPOLHTION USED BETWEEN
»»» LlNEr* INTEPPOLHTION USED BETWEEN
1 HPE SIMILftR OP INVERTED
1 WITH D50» 11.30 OMITTED FROM INTERPOLATION
2 HR£ ;IMIL*R OR INVERTED
2 WITH D54» =-.99 OMITTED FROM INTERPOLHTION
1.2731829 2.5384445
4.4999123 6.0392827
INTERPOLATED TO STD. INTEPVHLSs
VHLUES HT DlHM. MHPCED WITH • HR£ EXTR«POLHTED>
*.51 .-i3 1.69*001
1.00 3.51*401
1.25 3.52*001
2.50 6.32*001
6.00 1.55*002
10.00 7. 09*0OS"
15.00* 1.00*403
15.12
13.53
29.12
'Vi. 36
201.11
340.96
487.72
A-161
-------
»»» J'-ICHI-.TOP TE«iP., 4u5.i; -,-,•- JLD BE
"0 . OU 'Jl;« TO LIST THE OMTH trip Pljn: if.
HI Ijh
I~> TEMP.
TEST COMMENTS
.E DEM;IT,
QP n
. ON
PUN COMMENTS:
DMTE OF PUN:
-,TwPT TIME:
P'UN DUPnTION 'MINi
PUN TYPE:
• CHPBON DIOXIDE:
•. NITPOSEN:
•. O^YSEN:
'. WHTEP vftPOP:
&MCMJP FILTEP i.
j^TPHCTQP TCu . *T ;iTE PCM,:.
TCQMMx PMC, PCCftTEL'.G I&HHQ:
9M iir, • : PHQ* \, rjijij
PCOMMs PUN H-3-1
JD*TE= lui33i *«BIENT PPESSUPE 'IN Hi3.
1STnPT* 1520 iTftl> PPESi UPT HMBIENT 'IN i-
: OUP» 30.0 STftCc ii*S VELOCITY .FT-SEC'5
PTVP6» I STSCk TEMPEPHTUP£ . DEii.F''i
CD2* ».7 IMPHCTOP TEMPEPMTUPE 'BE'S F'!
CQ= .0 M*x. Prt&TICLE DlHM. itiiCPONij
N2= 75.4 Ci'CUQNE CUT ^DINT .nICPON;.:
Q2= 15.0 NQri'.E DIWnETEP • INCHES^ r
H3Q= 11.3 NQZZLE CUT POINT 'MICPQN;;:
' BF» ,E; L«fti3*!(>'• ENTEP •< OP N
P*PTltULhiTE DftTM PEDUCTION &ND ENTPV SYSTEM \\'ZZ'y* 13:56105
DMTM FOP TEST BY CONTPwCTDP TPU . HT :ITE FFMC. ON IlftTE I0£«i3j- PUN NO. 10
-.HMPLINiJ «T 130. i '. OF ISCH-INETIC PfilTE
.jnNT TO iEE PEiULTS USINiJ CLftSSICrtL 'STO^ESi DEF. OF Itlfm.f ENTEP 'i OP M
M
•»* LINEftP 1NTEPPQL*T10N USED BETIJE=M .36002583 .72445451
MftNT TO :EE PESULTi UilNS THE T5LD DEF. QF AEPO. DlwM.? ENTEP (" OF N
N
•-»• LlNEftP INTEPPOLATION USED BETWEEN .33002533
j^nT TO ;EE PE:ULTS USING MECCEPS DEF. OF nepo
ENTEP •< OP N
TOT.it MMSS 3.3734-001 3.573
-
".'i
PI
Tft.3E
CLONE
1
£
3
4
5
6
7
3
LTEP
»»»
• • »
.IP-*;F
MMSS
• MI5" '»
i3P •
'«;:
'13' DNCM>
341. •?>* Io53.o?
13.10
4.4£
3.58
3.33
13. 92
->.35
3.34
1.03
2.63
CUT POINTS FOP
MEftSUPED OfiTft
CUT POINTS FOP
MEftSUPED DftTft
^3.55
21.44
41.62
43.03
67.53
33.33
16.20
5.00
12.76
sTfwe s
FOP :T*3
STflGES
FOP ;TMG
6-001 7.5031+002 1.
DNC.F M
CUM. MKSS
• n>5' ONCM>
304. 3'?
340.34
21*. 40
177.73
134.71
67.18
33. *6
17.75
12.76
0 1 *PE
E» 1 WITH
1 2 *PE
E. 2 MIT"
G.MCM
D50
•MICPDNS*
13.27
12.12
10.71
7.17
4.32
2.72
1.37
.33
.51
SIMILKP OP
05 0- 12.
S 1 M I Lftf OP
D50» 10.
•*• LlNEnP INTEPPOL«TION USED BETWEEN .510337
INTEPPOLftTEO TO STO.
INTEPVfcL
;: 'VALUES
14.62
22,06
30.27
60.23
154.6*
324.21
344.31
*6 3 1+00 3
Mi3' DNCM
'3EO. ME3N
•MICPONS»
36 . 4 3
12.63
11.3*
3.76
5.33
3.62
l.*3
1.10
.67
. 56
INVEPTED
12 OMITTED
INVEPTED
71 OMITTED
21 .3
«T DlHM. nAPKED WITH
.63
1.00
1.25
2.50
6.00
1 0. 00
15.00*
DM AX- 100.0
MICPONS
DM-DLOGO DN-OLOiSD
'Ml3,DNCN> 'NO DNCMi
1,3'?+003 7. 47 + 007
1.61+003 1.51+00*
4.00+002 5.17+003
2.3*+002 6.7"3»»OS
2.50+002 2.35*00*
2.71+002 l.Cl'*+010
1.12+002 2.W+010
3.38+001 1.31+011
2.12+001 1. 35+011
4.24+001 1.72+012
FPOM INTEPPOLftTION
FPOM INTEPPOLSTION
777^216
» HPE EXTPHPOLiiTED^
2. 12+001
7.*2+001
3.3*-+001
1.32+002
2.5*+00£
5.00+002
1.00+003
A-162
-------
STA.'.t TE-16«AT
IroPACTQP TEMP'..
•~.~ .nQ'j^D if STAi> TEMP, "il
DO ,DU U1SH TD LIST THE DATA PHP CUN; -.met , QP M
DATA POP TEST Be 'SOriTSAiS TjP TP'J . nT SITE PP
TEST COMMENTS T-SOMMS PMC- FOCATELLO iD-
-t-ClHFK -I
PARTICLE DENSITY ii3M-'SC>: PHQ= 1. !).<•;
311 DATE lu
CALClrtERS
STAC-
PUN COMMENTS: PCOMM* BljN A-3-3
DATE OF RUN: JDATE» 103*83 Ai
START TIME: ISTAPT* 1727
PUN DURATION j'
PPESJ UPT AMBIENT 'IN K
SAi VELOCITY1 'PT iEC^ s
TEMPEPATUPE ' LES = • :
IMPftCTOP TEMPEPATUPE • DES P • 1
MAX. PAPTIULE DIMM. 'MlCPafli'
CYCLOME CUT PQIMT 'M1CPQM;'!
NQ"LE DIAnETEP . INCHED.:
iDiri.E "-UT POINT iniCPQN'>it
LAP'JP PAPTICLEJ ON PILTEP'
SUBSTRATES ID:
OESCP=PEEVEi ANSEL SUBSTRATE
CYCuQNE 34^.550 nG
STAGE 1 7.130
STAGE 3 4. aid
STAGE 3 b.S'SO
STAGE 4 b.310
STA.3E 5 :3.330
STAGE b
»TA.3E 7
,TAi3E
FILTER
4.550
3.aOO
1.5liO
"JO YOU '4ISH TD MODIFY ANY PIJN CONDITIOftS; ENTEP Y OP M
N
UAMT TO PETPIE'/E AMQTHPP PUN' ENTEP i OP N
n
DO Y'OU iJIiM TO TO PEDUCE THE DATA- ENTEP Y OP N
-5. 1!
•J?.rJ!
till.
FLOUi
IDSUBS=
PAPT1CULATE DATA PEDUCTION AND ENTPY V. ;TEM I J < ££ 5
DATA PQP TEST BY CQMTSACTDP TPg . AT ;ITE PPnC. ON DATE
:AMPLINi3 AT llja.l '. QF ISOKINETIC PATE
TO :EE PE;ULT; U;INS
DEF. OF DIAM..
iS. PUN NO. 11
ENTEP Y- OP N
M
UANT TO iEE PENULT' UilNiJ THE TiiLIl DEF. OF A£PQ. DIAM.. ENTER V CP N
•N
UANT TO IEE PENULTS u;iNi3 MEPCEPS DEF. OP A£PQ. DIAn.j EMTER t OP n
PUN A-3-i
TOTAL MASS i.osi^-ooi 5.bi03-ooi 4.0
GP • ACF GP • DNCF i*
STAi3E MASS MASS CUM. MA;;
• MG' 'MG-DNCM. 'MG-DNISM.
.-..CLONE 34*. 55 107---.57 304.33
1 7.18 31. Ob 173.33
3 4.*3 31.38 151. >i
3 b.51? 33.51 133.43
4 b-31 3»3.3b -"5.5«>
5 3.33 S5.oO ^O.f5
b 4.55 ff-.b* 41.37
7 3.bO 11.35 5u.u3
8 1.5* b.38 33.14
-ILTEP 5.35 33.14
**• CUT POINT; FOR STAGE; u i ARE
MEASURED DATA POP STAGE- 1 UIT*
•»» CUT POINTS FOR STAGES 1 3 APE
MEASURED DATA FOP STAGE. 3 WITH
INTERPOLATED TO iTD. INTERVALS: 'VALUES
35.50
34.5*
40.33
5*.b4
113. bO
lb-3.78
3b3.*3
403.74
a55» u 03 1 .
D50
• MicRnN'S*
13.00
11.45
10.13
•>-73
4.5>S
3.57
1.3u
.33
.48
SIMILAR QR
D5u. n.
SIMILAR OP
3338*003 DMA\a 100.0
MG--DNCM MICPONS
GEO. MEAN DM DLQGD DM DLOGD
•MICPON-SI 'Mi; DNCM> >MQ, DNISM
i4.b4 I.l7»0ul 5.3i:i»007
11.73 1.53*103 l.ic*uo1T-
10.77 i.="j»io3 ».ui+uiJi
3.38 I.b4*i u3 5.50*003
5..5b 1.5b*i 03 1.73*uo-i
3.43 1.43*iOe b.il + iJU*
1.33 b.bl»00l 3.uS*>Jli)
1.04 5.33*001 1f'.?7*ulO
-b3 3.a3*001 3.3u»ull
.34 7.b**o01 3.70*013
INVERTED
45 OMITTED FROM INTERPOLATION
INVERTED
D5u« 10.13 OMITTED FROM INTERPOLATION
AT DIAM. MARKED WITH • ARE EXTRAPOLATED/
.b3
1.00
1.35
3.50
b.OO
10.00
15.00*
30. 00*
3.85*001
5.76*001
5.01*001
1.13*003
1.33*003
3.?1*003
8.58*003
1.35*003
A-163
-------
DAT* FUP
T»- i -M8N
••.T»OU£XCFWC. ON t)AHSNXa26a3. SUM MO. 1
TEST COMMENTS TCOMM» FMC. POCATELLO IDAHOI C
•^LCINER =1
PARTICLE DENSITY 'SMxCOs PHQ» l.OOu
^ '=,2 AND QULET ONLY OF c
PUN COMMENTSs
DATE OF Puns
->TAPT TIME;
-UN DURATION
'UN TYPE I
PCOMM»
JDATE-
ISTAPT.
MINX: DUP»
PTYPE«
•- CARBON DIOXIDEi
'. CARBON MONOXIDE I
. -iITPOSENi
VAPORS
BACKUP FILTER
C02-
CO-
02 «
BF
;TACK i-
I Uc6MICPONS-»:
LAPSE PARTICLES ON FILTER?
H1PNS««*«1DEPSEN
MO. JETS
TYPE:
_ MODEL:
IMP. PLATE SET IDHPLATE*
MO. IMP. STAGES USED NS»
CUMDP '
.1638
.1253
.4100
.3830
.0533
.0343
PATE
SUBSTRATES ID!
DESCP«P6EVES ANSEL SUBSTRATES
. 033
.0000
.0000
.0000
.0000
.0000
.1760
.2940
.3050
156 .0254 1.0000
DP SCALINS FACTOR
.3600
.3620
.37*0
CYCLONE
»TAc5E 1
2
3
4 -
3
6
7
9
STAGE
STASE
FILTER
INTERPOLATE i*T
DI««ETEPS
.660
.600
.100
.380
.440
.370
3.680
6.710
1.030
.380
1.0
3x;DPJTK =
T iTSllK
DMAX»
DNOZZ»
CUTNQZ*
FLARSS-
FLQU»
139.0
100.U
13.4.
100.00
NO
3.0 10.0
DO YOU WISH TO WODIFY flNY BUM CONDITIONS"' EMTEP Y OP N
• n
UftHf TO PETPIEVE iWOTHeP PUM"? SNTEP Y OP N
•N
DO YOU WISH TO TO PEDUCE TWE DftTft7 ENTEP Y OP
DftTft REDUCTION KflD ENTRY VfSTEM 11x22x83 13136S03
D»Tft FOP TEST BY CONTRACTOR TPU . i»T SITE FFHC. ON DftTE 102683- PUN NO. I
•>»• i»S COnPONENTS NOP«»LIZED iO SU*» 100V., NOT 98.7
»T lia.8 •'. OF 1SOKIN6T1C HATE
TO SEE RESULTS USIN5 CLftSSICftL -STOKES1 DEF. OF DIftn.7 ENTEP Y OR N
.73237003
ENTEP Y OR N
.73237003
ENTER Y DP N
•N
•*» LINEAR INTERPOLATION USED BETWEEN .38241187
iJANT TO SEE RESULTS USIN6 THE T6LD DEF. OF AEPO. DIAH.7
-N
«••* LINEAR INTERPOLATION USED BETUEEN .38241187
.JANT TO SEE RESULTS USIN6 MERCERS DEF. OF ftEPO. DIAn.?
STAC" 2-5 SPUN C-l
TOTAL MASS s.ai4s-oe3
IS D30 '3EQ. MEAN
'MSI rniixDNCM^ 'MICRONS^ 'MICRONS^
CYCLONE .66 1.3d 2«.3» 13.39 36.59
1 ,60 1.26 28.13 11.59 12.46
2 .10 .21 28.12 10.25 10.90
3 .38 .80 27.13 6.36 8.38
4 .4* .?2 26.40 4.61 5.63
3 .37 1.20 23.21 2.60 3.47
6 3.68 7.72 17.49 1.31 1.33
7 6.71 14.07 3.42 .34 1.05
8 1.03 2.20 1.22 .49 .64
=;LTEP .38 1.22 -33
1 A»E SIMILAR OP INVERTED
1 «IT« 030- 11.39 OMITTED FROM INTERPOLATION
£ ARE SIMILAR OP INVERTED
e UITH D30» 10.23 OMITTED FROM INTERPOLATION
LINEAR INTERPOLATION USED BETHEEN .48818420 .33970147
INTERPOLATED TO STD. INTERVALS: "VALUES AT DIAn. MARKED UITH » ARE E>:TPAPOLATED>
1.3335-00* a.oi7o»ouj 3.0973*001
DMAX*
100.0
MICRONS
DMxDLOSD
< MS' DNCfl)
1.38*000
2.01*001
3.92*000
4.37*000
5.36*000
4.31*uOu
2.59*001
7.28*001
9.35*000
4. 04*000
DNxDLOSD
i (NQxDNCMl
6.18*004
1.99*007
5.78*006
1.48*0*7
5.75*007
2.21*008
7.85*009
1.20*011
6.30*010
1.88*011
CUT POINTS FOP STASES 0
MEASURED DATA FOR STASS.
CUT POINTS FOR ST»6€S 1
MEASURED DATA FOR STA5E*
2.22
9.79
16.3.3
24.94
26.98
28.71
29.9*
30.35
9,79
23.49
28.71
.63
1.00
1.25
2.50
6.00
10.00
20.00*
1.00
3.00
10.00
9.33*000
7.67*001
5.43*001
1.32*001
5.65*000
7.60*000
6.44*000
3.55*000
7.67*001
4.64*000
7.60*000
A-164
-------
DO ,OU '-ISM TO L'.ST T-IF L^T-i -jP P'JN: -:NIFP , DP 'i
[i^Tii =OC TEST E1. i".CNTPM,,TQP 7P'j , r- T SI"? P-'1C. 3N DHTE l.ji,.-. 3. -iJH NQ.
PUN COMMENT",: SCOMM= D.J!L
D*TE OF PUN: JDHTE* 14co
STftCT TIME: IST*PT= <.\
-ijH TYPE: PT'iPE» 0
'. SiiP'iON DIOXIDE: C03» i
' SAP BON MQNOMDE: C0»
' 'ilTPOSEN: 'I3= 75
' 0.. \i3EN: 03= 16
. unTEP V*FGP: HiO=> 15
t;*c«ijp FILTEP USED' »F= (ES
=LGU PATE DETERMINATION: METHO
E'lFnCTOP TYPE: IMPNi=tM*MNDEP
IIPHI'.TOR MODEL: IMP«OD«MHI
IMP. PLATE SET ID:IPLATE=
NQ. IMP. STASES USED NS»
'iQ. JETS DIlW. CUP1DP CALIB
io4 .1633 .4404 . 3u5o
364 .1353 .4404 .4034
364 . 4'?4>3 .4400 .41U4
364 .075? .0444 .3.354
?64 .0533 .0004 . io-'J
364 .0343 -1~60 .3640
364 .0354 .3'?"»0 .itaiO
15o .0354 1.0000 .3740
IMPSCTOP DP SC&LINi; PwSTOP
no iOu IJISH TO MODIFY I*NY PUN
N
MHNT TQ PETPIEVE flNOTHEP PIJN"
N
ET .i--;-ij'i C-i
-, I ^iMBUNT PPES",uP5 'IN ii^j
u^ STSC" PPESS uPT HME1ENT 'IN n3Qi
STMl",** TEMPEPnTljPE • DE'3 P>:
.5 IMPMCTO* TEMPEPPiTuPE • LEi; c'l
. ij rlH . . P^PTICLE DlHfl. 'NICPGNS':
.1 Ci'CLONF CUT POINT '"IICPHN'S ' :
. '? NQJZLE OInMETEP 'INCHES-':
.1 NOrTLE CUT POINT -MICPONS':
^P,;? PS.PTICLES ON FILTEP-
D=HHND CHUC
SEN IMP«CTQP FLOU PHTE <«CFM':
0 SU6STPMTES ID:
3 DESCP=P£E'VES HNi3EL SUBSTPftTE
CiCLONE 3.534 US
ST«*3E 1 ,3?4
* T hr»3E 3 .34 4
ST*3E 3 .334
STSH3E 4 .550
ST*3E 5 .?40
STSGE 6 3.300
ST*3E 7 3.750
.TPM5E 3 3.'?00
1.3.5" ^ILTRP 34.130 Mi;
CONDITIONS' ENTEP i OP N
ENTEP 1 OP N
P*MBNT= 15. "5
: uP STKi .43
TST*:U "l4^!i
TIMP= 153.3
DMft-.= lOij.ij
C1. CL» 13.J
DNQCZ» .135
CUTNOiT-a 1 04. uu
FLHPi36= NO
FLQI»l= -4T3
IDSUBS= 141
DO '.'OU Ul'.n TO TO fEDUCE THE D«T*T ENTEP V OP N
P«PTICUL»TE DftTH PEDUCTION HND ENTPY SYSTEM 11 33-33 13:56105
DnTn FQP TEST BY CONTPnCTOP TPU . nT SITE FFMC« ON D*«TE 1436S3« PUN NO. 7
*»» i5rti COMPONENTS NOPM«(_I7.ED >0 SUM» 144'.. NGT r"i.3
SSMPLINS HT 144.1 V OF ISOKINETIC PSTE
WMNT Tn SEE PEiULTS USINi; CLnSSICHL 'STQKEi< DEF. OF DISH.' ENTEP Y OP N
>N
lUKNT TO SEE RESULTS USINS THE TGLD DEF. OF i=tEPa. DlftM. . ENTEP 'i OP N
: N
y*NT TO SEE PEiULTS U.SINS MEPCEPS DEF. OF d€PQ. DlftM.' ENTEP V OP N
OUTLET .3-3SPUN C-3
TOTHL MHS.S 3.365;
.Si'CLONE 3.5S
3 .34
4 .55
5 .*8
7 3.75
=ILTEP 34.13
•*• CUT POINTS FOP STiWES 0 I *P= S11ILt»P DP im/EPTED
MEH-SUPED DHT« POP STPHie. 1 i^ITH U50» 11. I? OMITTED FPOM INTEPPOLHT ION
•*• CUT POINTS FOP STSI5ES 1 i HPE SIMILftP OP INVERTED
MEftiUPED DftTft FOP iTf*>3E. 3 UITH 054» ^.S? OMITTED FPQM INTERPOLHTION
INTEPPDLftTED TD STD. INTERVALS: 'VfiLUES i*T DIi*M. MftPKED WITH «• (WE EXTPftPQLHTEDJ
3.5363-403 5.133'?*001 3.0?33*001 DMi=iX» 100. u
'SP'DNCF Mi5^HCM MG DNCM MICRON'S
MHSS CUM. MASS D50 i3EO. MEHN DM^DLOiSD DN- DLOGD
- DNCMi
4.73
. 73
. 37
,5*
1.03
1.33
5.1?
5.10
5.38
55. ?5
MI; - DNCM >
76.14
75.43
75.04
74.45
73.43
71.63
6o.43
61. 33
55. ?5
•MICRON'S}
13.40
11. !•?
•?.3?
6.63
4.45
3.51
1.37
.31
.47
•MICPONi
36.06
1 3 . 46
14.53
3 . 0«
5.43
3.35
1.73
1.01
.63
.33
'Mi;. DNCMi
5.40*4uo
1.11*441
O.1?!*!)!)!!
3.40*000
5.'?c*000
7. 30*4u4
1.74*001
3.64*001
3.38*001
1 .36*003
' NO DNCM'
3.34
1.31
1.14
1.33
7. ''11
3.73
5..J7
4.35
1.35
•?.60
4U5
007
007
047
UO 7
U43
uO1?
4 1 4
Oil
413
63. *4
6o.3o
71.5*
74.34
75.4*
7«i.53
,_77.36
1.00
1.35
3.50
6.40
14.44
15.04*
3 4 .44*
3.66*441
3.31*401
1. u5*44l
5.3?*444
5.74*444
6. 33*OuO
7. 45*404
A-165
-------
TO ._l;T TNC
-OP PUN: -NTr'
QP '1
CONTefti; TQP TC,g , ^T ilTF
TCOMn» = MI;. = OCATEL^ I
-•iKTICLE
>-:jH COMMENT;;
DATE OF PUNS
-,TAPT TIMES 1
PUN DURATION 'MIN.<:
*UN TYPES
• CARBON DIOMDE;
CAPBON MONOXIDES
• NITROGEN;
Qh DATE lui^.ji. FUN nQ. ;
CALCINE?; :>,= ~ti\j CULET QNLI OF r
=C2MM= OUTLET i-5! PUN C-3
JDATE= 1056i3 AMBIENT PPECiUPE 'IN Hi5 . FAMfc'-iT:
;TART= 1^4; ;TAC>> PRESS UPT AMBIENT .IN Hio.sDp;Tk=
DUP» r>U.O STACk '7*; VELOCITY 'FT-JEC'S VST SCI"
PTYP6" 0 STAC" TEMPERATURE ' DEi3 F.I TSTSO =
CD»
Ncf"
.0 nftx. P«*TICLE Dlftfl.
r^.l C'< CLONE CUT POINT -
16. r1 MQZrtE BlnMETEP ' IM
li.5 NOZr'.E CUT PQIMT
' BF» YE;
iTIONS METK
&ACI-UF FILTER U.SEI
1MPACTOP TY'PE:
IMPACTOR MODEL: 1MPMQD»MIH
IMP. PLATE ;ET IDHPLATE=
NQ. IMP. ;TAi3Es U;ED N;»
•'0. JETS DIAM. CUMDP CALIB
564 .1638 . OuOO .3050
564 .1553 .0000 .4030
5^4 .0*48 .0000 .4100
564 .075? .0000 .3850
i^4 .0533 .0000 .36*0
564 .0.343 .1760 .3600
156 .0554 1.0000 .5740
IMPACTOP DP ;CALINl3 FACTOR
L«Pi3E
ON
IB:
Cn'.'-ONE
1TA.5E 1
;TA«E 5
iTA^E
;TA>SE
FILTER
1.570
.560
.080
.140
1.510
3 . 01 0
1.370
LO YOU WISH TO MODIFY
N
iJSMT TO PETPIEVE MNOTHEP PUN
N
PUN CONDITIONS? ENTER v OP r)
ENTEP i OP N
TIMP=
CYCL"
CUTNO;
I 0 i"J . 0
li.5
1 0 u .
no
IDiUBS"
DO YOU WIJH TO TO SEDUCE THE
ENT^P Y OP
E DMTM PECUCTION niND ENTPY ^'
D»Tfi FOP TEiT B'(' '-.QNTPfHlTOP TBU • ftT ;I
•»» >3Hi COMPONENT! NOPMfcLIIED »D SUM
'.MMPLlNi; i*T ll'r-.S '. OF I10VIMETIC
'JMNT TO iEE PEJULTS USIN6 CLM
100X
:^ DEF. OF
ll,ii-:53 13156S05
ON DftTE 10568.3. PUN NO. 8
NOT '?8.6
«-»» LINEf* INTEPPOLftTION USED BETUEEN .38815505
••• LINE&P INTEPPOLftTION UCED BETUEEN 4. 51100«8
TO ;EE PEiULTi UilNU THE TSLD DEF. OF *EPO. DIMM. •
»» LINEftP INTEPPOLftTION USED BETUEEN .38S15505
-» LlNEnP INTEPPOLHTION USED BETUEEN 4.511CllJ?p3
TO ;EE PENULT; uiiNS MEPCEPS DEF. OF I^EBQ. DII=>M. •
ENTEP i OP N
6.7575410
ENTEB f OP N
. 7-3:3 3'?*<:^
6.7575410
ENTEP Y OP N
OUTLET 5-5S RUN C-3
TOTAL MA;.; 1.50.35-005 5.3744-005
SP'ACF SP'DNCF
.45
1.57
.56
3.4400+001 5.4134+001
Mfl'ACH MI5--DNCM
DMAX» 100.0
MICRONS
i.YCLONE
1
5
3
4 .08
5 .14
6 1.51
7 3.01
8 1.37
FILTEP 14.?o
•** CUT POINT;
MEASURED DA
+•» CUT POINT; FCIR i
MEASURED DATA FQR
»»» LINEAR INTERPOLAT
INTEPPOLftTED TO STD. INTERVAL
MAii
>xDNT.M>
,'fl
5.74
1.51
4.1>>
.17
.30
3.56
6.4?
5.^6
35.14
;T»SES
CUM. MA;;
' Mljx DNCM >
5.3. 4J
50.6?
4?. 48
45.35
45.15
44.34
41.5?
35.0?
35.14
0 1 APE ;
OP ;TASE. i UITH
STAOT;
QR ;TA
ATION
NTERVA
i 5 APE ;
>3E> 5 UITH
J;ED BETUEEN
L;I 'VALUE;
35.31
38.04
41.05
44.. 74
45.56
50.31
54.50
54.33
D50
ijEO. MEAN
DM-DLOGD
• MICRONS* ' MIGPON;* 'Mt5x[iNCri>
13.55
11.60
10.55
6.86
4.65
5.60
1.31
.84
.4?
IMILAP OP
D50« 1 1
IMILAP OP
050" 10
4.6177
AT DIAM.
.63
1 . 00
1.55
5.50
6.00
10.00
15.00*
50.00*
36.77
15.55
10. ?0
8.3?
5.63
3.47
1.85
1.05
.64
.35
INVERTED
.60 OMITTED
INVERTED
.55 OMITTED
1.04+000
4.11+001
... 56+001
,..3?+001
.00+000
.51+000
,0?+001
3.36+001
1.55+001
1.07+005
DN DLOGD
•NO' DNCM.
4.00+004
4. ijO+007
3. 35*007
7.73+007
1.07+007
5.56+007
3.31+00?
5.54+010
?. 11+010
4.?5+015
FPOM INTERPOLATION
FROM INTERPOLATION
163 6.36438?4
MARKED UITH
» ARE EXTPAPOLATcD>
1.15+001
3.55+001
5.46+001
5.16+000
1.00+000
5.68+001
?. 74+000
_ rt 0
A-166
-------
APPENDIX B
FIELD DATA SHEETS
-------
APPENDIX B-l
TRAVERSE POINT LOCATIONS
-------
TRAVERSE POINT LOCATION FOR
DUCTS
1ANT.
r/n
-------
TRAVErtSE POINT LOCATION FOR CinGULAft DUCTS
PLANT
DATE
SAMPLING LOCATION A
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR D^ /
312:
,1
>L
-
-
—
—
-
...
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
A-^
A-*
C-3
c. •*
FRACTION
OF STACK I.D.
STACK I.D.
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
30. V5L
4t , ar
ffO • f*
*/ ,ar
^
DISTANCE B
3
TRAVERSE POINT LOCATNJ
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
EPA (Dur) 232
4/72
B-4
-------
TRAVErtSE POINT LOCATION FOR
DUCTS
T\f (__
,L.«T F Mfl .r1. .
,.TF CMTfTP- : •. .' .r . . "
JAI L
iANIPLING LOW
NSIDE OF FAR
OUTSIDE OF
NSIDE OF NEAR
OUTSIDE OF
[TACK I.D., (DIS
IEAREST UPSTF
IEAREST DOWNS
IALCULATOR J
TinN £ -
WALL TO
NIPPLE, (DISTANCE A)
WALL TO
YIPPLE, (DISTANCE B)
TANCE A - DISTANCE B
?EAM DISTURBANCE
;TREAM DISTURBANCE
DM 7^
'^-) A.-^ ;J^H-
•t • .
91
* .*T
TRAVERSE
POINT
NUMBER
/
3L
3
->
1
?
10
//
IOL
FRACTION
OF STACK I.D.
STACK I.D.
?8"
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
y.o?
/a.*r
Pd.VA
py^s^
36,-^r
H,?A
53. or
b/,*S
ti, ..r*
^y. -?r
^3^«-
.
311 m at
• • i
1UI >
•.« I
•-• •
M^l U
--» «
:::;[
~~ f.rr
T-T^T[
BLt Hffn
a.m
a-»
•.a
IV.*
•Ji
m«
SCHEMATIC OF SAMPLING LOCATION
DISTANCE B
TRAVERSE POINT LOCATION
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
i
'A (Our) 232
4/72
B-5
-------
TRAVErtSE POINT LOCATION FOR «W6UfcAft DUCTS
PLANT.
rnt-
SAMPLING LOCATION
S
~ENTE*
: OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR i>AS to
•fp
J}
—
—
— 1
-
-
—
—
--
—
—
—
.._
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
A-i>
A- %
£-3
C -9
FRACTION
OF STACK I.D.
?»"
STACK I.D.
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
0o. va
£/ ,sr
P0< Vft
tt .&r
•
DISTANCE B
0*7-**
£+r9-*
g^^^* j^^^T^^^
^.f y ^5
TRAVERSE POINT LOCATIOI
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
EPA (Dur) 232
4/72
B-6
-------
TRAVErtSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT.
iSAMPLING LOCATION gut lt.t V
INSIDE OF FAR WALL TO
1 OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR _£flS
Ai-y
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
/
2
3
V
5-
*
7
J
7
/o
If
/a
;s
/V
/y
/6
FRACTION
OF STACK I.D.
9*. i
STACK I.D.
0*,l
/
I
1
1
1
I
1
1
1
1
I
j
V
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1, 8 INCH)
/•3
3.9
6.,?
1-1
/3.*
;->.y
aji, 5"
Q1.S
-------
TRAVErfSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT
DATE
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE,
CALCULATOR.
F\jrrp-r-
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
+-* fl'l
t-AA-fl.
•6 B-l
fl.ft
FRACTION
OF STACK I.D.
STACK I.D.
?r,/
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
//,,<,
n .3
£?,<£
*
DISTANCE B
TRAVERSE POINT LOCATIO
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
-
EPA (Dur) 232
4/72
B-8
-------
EPA METHOD 1
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT.
DATE _
/U bb*-
SAMPLING LOCATION .
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE. (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE. (DISTANCE B) _
STACK 14.. (DISTANCE A • DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST OOWNSTREAttZIISIRJfi&ANCE.
CALCULATOR _p^liil_l
±£P
/
OISTMCIJ
FtW IIC1M Of flKl. ti»dM)
«.««
-TzT
s.M
».2S
f.25
12.31
wirj
17. (I
».
If.
II.
II.
1).
II.
IS.
l«.
JJ.7J
ST.JJ
»1.I3
•'•»
»'.J>
«*.««
".»
Ucitlo *•«•»
fn» iMMl »f «t»ct »»^"1
I. II.K
2. U.M
SCHEMATIC OF SAKPLJNG LOCATION
TRAVERSE
POINT
NUMBER
f
2.
-I,
A.
/'
u2 / * a
7O '/4 ''
^7 ^i ^ //4."
EPA (Out 22
4/7Z
B-9
-------
EPA METHOD 1
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PUNT.
DATE _
IT f n r- -
SAILING LOCA
INSIDE OF FAR KALL TO
OUTSIDE OF NIPPLE. (DISTANCE A) _
INSIDE OF NEAR *ALL TO
OUTSIDE OF NIPPLE. (DISTANCE B) _
STACK {St., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST OOWNSTRE
CALCULATOR.
T»A»nJ?k/2."
1
4/7Z
B-10
-------
EPA METHOD 1
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT.
DATE j
SAMPLING LOCATION .
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE. (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE. (DISTANCE B) _
STACK ID.. (DISTANCE A • DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
CALCULATOR _IUJ6_
/- i -2-
m»r»ss
rut*
f
i.is
3.S3
(.35
».jj
12.31
K.IS
I0.7J
77. »3
DISTANCM
Of n*C». (li
IV.
II.
II.
13.
14.
IS.
JJ.7J
17.»
• 1.13
W.J!
fl.lt
tf.tl
7i. n
n •^•TMK r*ut>
I. II. »
I. »I.H
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
1
2
3
4-
^
Q,
1
9T
^
lO
i\
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^
I-'i
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^ <*± 11$ •»/*"
—
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65 A Co 3 '/4.1
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-••'.•».. n"»,M*"
->«:. ^ r?S'7Af^
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EPA (Don a:
4/7Z
B-ll
-------
APPENDIX B-2
PRELIMINARY MEASUREMENTS
-------
PRELIMINARY VELOCITY TRAVERSE
i
I
i
'i»rr h /*\ VJ
LOCATION iVU / J= r i5 -i. 4
STACK LD. 51 X >
TRAVERSE
POINT
NUMBER
fi - 1
S
3
/ .V
;,1
. So
.«ro
. V9
. 3o
.5-3
, 551
5. »
S>, /
l.f
7.6
/ 0
l-l
5T
. ; r
.15-
, 3*
.#
. ^r
/-oS;
STACK
TEMPERATURE
fT,). T
S6£
cor
^•>v
V0<.
*r 79
Ky
S?
•T fi
<,9a
^ ff
Viy
^70
V3
V*i"
V7A
'fft,
V90
^,
501
yoo
STACK
TEMPERATURE
(T,), 'F .
%3
(,5,-;
*f •)!
V ? /
v ^->
Ma
v?3
s s- f
i^3
v?o
?-?
-------
i-^ r*i v
r
PRELIMINARY VELOCITY TRAVERSE
PLANT _
DATE _
LOCATION .
STACK LD..
-o72*
' BAROMETRIC PRESSURE, in. H|
' STACK GAUGE PRESSURE, in.
OPERATORS
TRAVERSE
POINT
NUMBER
o
'
,7
AVERAGE
J
iPA(0«ri233
4/72
VELOCITY
HEAD
A 96
.P
STACK
TEMPERATURE
5-51/
<$*
111.
li-
SCHEMATIC OF TRAVERSE POIKT LAYOUT
f
TRAVERSE
POIHT
NUMBER
/o
i
sr
AVERAGE
VELOCITY
HEAD
/.e*
AC.
./J?
STACK
TEMPERATURE,
a,), -F «i
ST3S
S30-
B-14
-------
tNVinONMCNTJU. tNGINtlRING DIVISION
I r/v
1-4. 5
NOMOGRAPH DATA
PI .NT
SAMPLING LOCATION .
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20*F). *F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in H|
STATIC PRESSURE IN STACK, in. H|
(P,,±0.073 i STACK GAUGE PRESSURE in in. HZ0)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD. m. HjO
MAXIMUM VELOCITY HEAD. in. HjO
C FAaOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, m.
REFERENCE ip. in. H20
AH,
T"»,.
•w
Pm
Ps
"'P.
Tw
^»«.
4P«.
££>
-to
IL-.I -
25^5
"2-S 15
.^
,^c.
'-Ct3
^
EPA (Our! 235
472
STn
B-15
-------
TRW
tnWfiONMCNTM. fNGINSfRING DIVISION
EPA METHODS 1-4, 5
NOMOGRAPH DATA
PLANT
DATE
SAMPLING LOCATION
EPA (Dun 234
472
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°F)."F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Kg
STATIC PRESSURE IN STACK, in. H(
(Pm ±0.073 i STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD. in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE ^p. in. H20
AH.
T™avi.
B«0
P.
Pj
P'P
rm
savf.
*»«|.
A'«.
/, 7 '<
ut£
/D
2$tf
-4,S
fll
.5&
j.rt
2, ok
J
_J
B-16
-------
TRW
INVIfiONMENTAL CNGINCERING DMS10H
PLANT
DATE
EPA METHODS 1-4, 5
NOMOGRAPH DATA
SAMPLING LOCATION
"
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F), »F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 i STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD, in. HjO
MAXIMUM VELOCITY HEAD, in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE .ip, in. H20
4H$
mavg.
BWO
PR,
ps
P«P
rm
savg.
APivg.
^Pnax.
.1
.'^
•>
• 1
inf
fiO
/&
25.
-------
NOMOGRAPH DATA
PLANT
DATE.
r
SAMPLING LOCATION
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
1
AVERAGE I5IETER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hj
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD, in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
AH@
T|nav«.
Bwo
pm
PS
P'/P.
S3V».
^Pavg.
*P«a.
p.fr
/oo
/'o
£$.!&
-g^*Hs
M
€*>7
l.o*
£,ob
l./f
.n$
•nt
£.*i
EPA (Dur) 234
472
B-18
-------
NOMOGRAPH
PLANT.
DATE_
SAMPLING LOCATION
./Jfe
e-s
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H£0
1
AVERAGE METER TEMPERATURE (AMBIENT* 20 0F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. tig
STATIC PRESSURE IN STACK, in. H«
(Pm±t).073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
*H@
Tmavg.
Bwo
P.
ps
P'/pm
savj.
AP»|.
*P,nax.
Mt>
Id
10
**.-)*>
— S.^fr
W
63H
f.*8
3.o*>
A/5*
j^S^S^f^
tH^fl^^V
;y/4
o£ SQpt^
EPA (Dur) 234
472
B-19
-------
TRW
I ONMfNTAL CNGINCERING DIVISION
NOMOGRAPH DATA
PLANT /-
DATE "
SAMPLING LOCATION .
X:
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREW/I BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hj
STATIC PRESSURE IN STACK, in. H(
(Pro±0.073 i STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE V-.LOCirr HEAD. in. Hf
MAXIMUM VELOCITY HEAD, in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE ^p. in. H20
iH&
T|"av{.
Bwo
pn
PS
s
Tw
A"a«i.
•iPmai.
.J
,J
c.
/.-'!
110
/C
^.^
~%,r<
.97
.tt?-
s,w
./e
FT.K
te
/?
?*
EPA (Oui! 234
472
B-20
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT
DATE
LOCATION .
STACK 1.0..
Ff>vC
fe —
f BAROMETRIC PRESSURE, in. HI 25-
STACK GAUGE PRESSURE, in. H.n - f //>
BPFBATQBS Ofe I I-/"—
SCHEMATIC OFTTMVEHSE POINT LAYOUT
,\
TRAVERSE
POINT
NUMBER
X? "7
VELOCm'
HEAD
(as,). in-HjO
/.3o
.ss
.30
/*-
AVERAGE-
.Tn
1L
.OS
.10
STACK
TEMPERATURE
fTJ /
.-537
TRAVERSE
POINT
NUMBER
/a
yy
3
AVERAGE.-
VELOCITY
HEAD
IK,), m.HjO
/.-ft,
/.J3G
STACK
TEMPERATURE
ai. -F
1 Y
B-21
-------
NOMOGRAPH DATA
PLANT r i'\ ^
DATE r j / *; -i
SAMPLING LOCATION *' ' /
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE lilETER TEMPERATURE (AMBIENT + 23 CF),8F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pn,±f).073 i STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
AH@
Tmav«.
Bwo
pm
ps
V.
sav».
Afw
APmax.
1 I C5
/ c
OS ^~
•• » — '
i
'i . ; i
, ••> -l
i "•>
J.I
'^fS . 3L$"O
, & .1^
0#?c/)le.
EPA(Dur)234
472
., 1 -1 - C.
B-22
-------
NOMOGRAPH DATA
PLANT
SAMPLING LOCATION £ " /
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 VF), "F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD. in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
AHe
Tmavg.
Bm
Pm
ps
Pvp.
savj.
^Pavg.
^Prrax.
/.•?/
lin
/o
<5:f .?o
-?.o
.7?
S'3D
.%s
I'Z
'• 1
,*#K2i , ( ar >"
, • J O
3.o
EPA (Our) 234
472
* ±
B-23
-------
NOMOGRAPH DATA
PLANT
DATE.
•'.- / ' ' r
•"< V-
SAMPLING LOCATION
5<>'
/? / ,1
2^L
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 200Fj,°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20 _
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
4H@
Tmav«.
Bwo
^
Ps
P*/p.
savj.
*Pavg.
*PMx.
!.f
kAX^ .W^J.rt
I It ^
fl / 0 T
*.£
EPA (Our) 234
472
B-24
-------
PRELIMINARY VELOCITY TRAVERSE
c"V.~ ^
Cbi &''« ^
DATE
LOCATION C • * i :
STACK I.D.
BAROMETRIC PRESSURE, in. H|
STACK GAUGE PRESSURE, ii. 1U>
f- a a
I ft
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
HUHBER
Pi- ^
-.
T
I
,l-
(-
/-- 1
-_
*
s
--
(_.
T^=-
AVERAGE
VELOCITY
HEAD
la*,).in.HjO
/. ^
1.-^.
/
-------
+» ''- TRW '
tMKOMHfNTM. IHGlNlVtlMS DIVISION
FIELD MOISTURE DETERHIHATIOH
Location rVflf-i Z- 2. ( Pm £\fCJ
Test
Operator l4gM ft.-
Date io),9M|v*>
By Absorption:
Barometric Pressure-?.b- ? o
D
6/%,
T" J J
/D /^ .,
/ >' ' c ^
3c (0
Meter
^b-J.^^T
•2b3 D^r
^ b '7 fe I D
.57/.if6t/
^.^ r
Flow Meter
Setting (-SFH-)
" (+T.O
/. w'-
y. sa
AfrX '•
/,^^
Meter
Temperature, Tm
•r-j
Jf^-
^
5-^
• 5" 7
-------
TRW
tNVIKONMlNTM CNGINCCRING DMS1ON
PLAHT
EPA METHODS 1-4, 5
NOMOGRAPH DATA
SAMPLING LOCATION
CjZ^lKS^^
0 / " '
£-fcch 2-2^ L_
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. HjO ,
AVERAGE BETER TEMPERATURE (AlflBIENT + 2D*F).*F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, m HI
(Pm±0.073 I STACK GAUGE PRESSURE in in. HZ0)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD, in. MjO
MAXIMUM VELOCITY HEAD, in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
AHt
T™1V|.
B«o
Pm
Ps
P'PB
*JV|.
4»H|.
A»nni.
.•%!
^2- A>-t**j
IV-
3- j
i.%^-
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1C
i^oer'
iS.Xf
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is.qr'Hc,^
j
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tf»
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EPA (Our! 234
472
HP
B-27
-------
TRW
INVIRONMCNTM. IHCINtlRIHG DIVISION
v
EPA METHODS 1-4; 5-
NOMOGRAPH DATA
PLANT.
SAMPLING LOCATION
Hiff
2~?
EPA iD'jrl 234
472
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. HjO
AVERAGE METER TEMPERATURE [AMBIENT »ZO*F).*F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hf
STATIC PRESSURE IN STACK, in. Hf
(Pn±0.073 i STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. "F
AVERAGE VELOCITY HEAD, in. HjO
MAXIMUM VELOCITY HEAD. in. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE -ip. in. H20
AH,
T»JV|.
B*o
P»
Pj
VP.
T'«,
«*|.
*P«.
'^"" ,
-1^
70
l^-o
I^S
?-. A~L.'^°
I.eo
IW-2?
\^
'•" L^
\TS>
B-28
-------
TRW
tNVaOMMlHTM. IHGIHICRIHG DftOION
PLANT.
OATE_
EPA METHODS 1-4, 5
NOMOGRAPH DATA
SAMPLING LOCATION O L/f'&!
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. HjO
AVERAGE METER TEMPERATURE (AMBIENT + 2D*F),*F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. H|
STATIC PRESSURE IN STACK, in. H|
(P,±ll.073 > STACK GAUGE PRESSURE in n. H;0)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD. ui. HjO
MAXIMUM VELOCITY HEAD, w. HjO
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. h^O
AH^
T-«,.
B..
P.
P,
"'P.
Tw
a»,n
*>m.
n
te
.^
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f.VZ
yo
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25.7^
Ml"^
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IHD
• U
/.A
^
^
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?
EPA iDur! 234
472
B-29
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT
DATE
LOCATION "V^
STACK 1.0
BAROMETRIC PRESSURE, in. H|_l:
STACK GAUGE PRESSURE, in. H20_
OPERATORS Kfc.N.^\/ / 6
•M
*6
TRAVERSE
POINT
NUMBER
A--'
/V-T-
.V?
jOf.^-
K-r
*•&
&-1
A: S
A-f
rt--'d
/(-•//
/V-/7_
t*--'j
fi-fv:
f^-t f
/V -^
AVERAGE
VELOCITY
HEAD
(4»5), m.HjO
.So
-*( S-
. frC*
. T5
, f 0
-S3'
'S5
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,^
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/,!D
I'SC
/.or
1,1$
}• 10
,, 0
-^
STACK
TEMPERATURE
a,i. *F
3^1
S^<-(
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's €>6
9 S«r
^5.^
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rs'J
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Qd£.
3! 9
W<:
d£>(
1.^^-L^
SCHEIIATIC OF TRAVERSE POINT LA
TRAVERSE
POINT
NUMBER
B-/
* 2
c 2
c_v
XP.i-
5 -4
8"f
S-'S
G-/C
AVERAGE
VELOCITY
HEAD
/,>o
. 13
. fi'
,->r
,/ f
•
.Rtf
STACK
TEMPERATURE
(Tsl. -F
3e?
^,3^
<3o -5
3 > (
• 5 ' 1,
£3 /
.P<3T
3 ?0
Jj-j"
3 39
3/F
3=0^
3s 9
1 1 •»
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•^63
I
7.C|4.t^
EPA (Our) 233
4/72
B-30
-------
r- -. -,
h "- '- '
r'i\Li
.••;*—
NOMOGRAPH DATA
PLANT
DAIE
SAMPLING LOCATION .
®i-
<&L-
I 5
I ^
CALIBRATED PRESSURE DIFFEREfiTIAL ACROSS.
ORIFICE, infh20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. tig ' >•
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
(VMIS! i^i/JX
C FACTOR
A
CALCULATED HQ^E DIAMETER, in.
,:j^
ACTU'AL NOZZLE DIAMETER, in. /^^j-f\
REFERENCE Ap.Yi. H20 ^^ '
AHg,-
Tmavg.
BWO'
pm
"^
Ps
'%
/r>n
savj.
APavg.
^Pmax.
A-l-Y
G?£> '
:^^
iLC^.t
Irl^^
l.otf
I'^r"
^4-
I.X5"
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.^°.
,2.1^7
^l«4 V'^s
SL
"{irtr 7
EPA (Du;l 234
472
B-31
-------
NOMOGRAPH DATA
PLANT.
DATE_
SAMPLING LOCATION
& fv
.IS"
EPA (Durl 234
4 72
/I
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F), °F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, "F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VFLOCITY HEAD in H*0
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCED, in. H20
AH,
T™avg.
Bwo
pn,
Ps
°m
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60
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B-32
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PRELIMINARY VELOCITY TRAVERSE
?UNT_
LOCAT10H
STACK I.D.
BAROMETRIC PRESSURE, in. H|
STACK GAUGE PRESSURE.*. H
SCHEMATIC OF TRAVERSE POINT L>YQUT
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POINT
NUMBER
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7X
B-33
-------
NOMOGRAPH DATA
PLANT .
DATE/
SAMPLING LOCATJON .
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE I AMBIENT -i- 20 *F).*F
PERCENT MOISTURE IN GAS STREAM BV VOLUME
BAROMETRIC PRESSURE AT METER, in HJ
STATIC PRESSURE IN STACK, in. H|
lPm±0.073 i STACK GAUGE PRESSURE in m. H20|
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. "F
AVERAGE VELOCITY HEAD. in. HjD
MAXIMUM VELOCITY HEAD. in. H^O
C FACTOR
CALCULATED NOZZLE DIAMETER. •«.
ACTUAL NOZZLE DIAMETER, in. /"l Q 1 )
REFERENCE is, in. H20 ^" "^
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NOMOGRAPH DATA
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OATE_
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AVERAGE METER TEMPERATURE (AMBIENT + 20 °F),0F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AUPRAPP UPI nrrrv HFan in n n
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C FACTOR
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B-35
-------
APPENDIX B-3
EPA METHOD 5 - STACK FIELD DATA SHEET
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APPENDIX B-4
EPA METHOD 5 - SAMPLE TRAIN RECOVERY SHEET
-------
TRW
EPA MrTHOD 5
ANALYTICAL DATA
PUWT.
SAMPLING LOCATION
SAMPLE TYPE ***
RUN NUMBER _^lZ
SAMPLE BOX NUMBER.
CLEAN-UP MAN _^lt.
COMMENT!
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASH. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
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CONTAINER ,
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BACK HALF
MPINCER CONTENTS AND WATER WASH OF
HPINCERS. CONNECTORS. AND BACK *
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MOISTURE
•PINCERS
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KCT VOLUKE
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F«AL «IGHT <•
INITIAL WEIGHT
•ET niGHT
CONTAINER
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EXTRACTION
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TOTAL WEIGHT
_«i
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TOTAL MOISTURE.
B-72
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
DATE _i£_J_L_2_2_
SAMPLING LOCATION ?•*"
SAMPLE TYPE faTJ't d
RUN mniBFg /? • 2,
SAMPLE BOX NUMBER
CLEAII-UP IUN
COWEMT&
1-
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FLASX. FRONT HALF OF FILTER HOLDER
FILTER NUMBER *^f~ 6\j^JjJ^§ CONTAINER .
LABORATORY RESULTS
.•I
FRONT HALF SUBTOTAL.
BACK HALF
UPINGER CONTENT! AND WATER «UH OF
WRINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINCER1 CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
-it
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\
MOISTURE
WINGERS
FINAL VOLUME 7 2 ^
INITIAL VOLlfl
MET VOLUME
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INITIAL WEIGHT
RET WEIGHT
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TOTALaoimmE llo.
B-73
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT.
OATE_
lo -
SAMPLING LOCATION Sf •
SAMPLE TYPE.
RUN NUMBER.
A-
SAMPLE BOX NUMBER
- "T
COMMENTS:
FRONT HALF
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FLASK, FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER .
LABORATORY RESULTS
*
FRONT HALF SUBTOTAL.
BACK HALF
HPINCER CONTENTS AND IATER WASH OF
WRINGERS. CONNECTORS, AND BACK *
HALF OF FILTER HOLDER
ACETONE f ASM OF IMPINCERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
•PINCERS
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INITIAL «ni IMP
NTT VOLUME
auu ca
FWAL WEIGHT "-
• INITIAL WEIGHT "^ '- I
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CONTAINER
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CONTAINER
BACK HALF SUBTOTAL
-»i
."•I
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TOTAL WEIGHT
TOTAL MOISTURE
B-74
-------
PLANT
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN-UP WAN
ANALYTICAL DATA
j«»rx. •/
FRONT HALF
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FLASK, FRONT HALF OF FILTER HOLDER
FILTER NUMBER
O.&SZ/o
COMMENTS:
CONTAINER * J
CONTAINER .
LABORATORY RESULTS
__ "I
FRONT HALF SUBTOTAL.
BACK HALF
KHPINGER CONTENTS AND WATER WASH^OF
IMPINGERS, CONNECTORS, AND BACK
HALF OF FILTER HOLDER.. ' '^
1
ACETONE WASH OF IMPINGERS, CONNECTORS,
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FXTRACT"1" _ , ,
CONTAIflFR
BACK HALF SUBTOTAL
TT1TAI WFIGHT
Df
: Blf
nt
at
MOISTURE
IMPINCERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA CEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
EPA (Our) 231
4/72
TOTAL MOISTURE
B-75
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLA«T
HIT* yfe*- I 7-
SAMPLING LOCATION 5<~f~
SAMPLE TYPE fl'"fVl*o d
RUN MMME» ./?- /
SAMPLE BOX NUMBER.
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LABORATORY RESULTS
FILTER NUMBER
CONTAINER.
CONTAINER .
FRONT HALF SUBTOTAL.
BACK HALF
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•P1KGEK
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autuca
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TOTAL WEIGHT
_i»i
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3. 5
B-76
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
P /tic ~
- 2 *? -
COMMENTS:
DATE.
SAMPLING LOCATION S<^><~ M
SAMPLE TYPE /?V/7
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT.
OATE_
SAMPLING LOCATION :
SAMPLE TYPE jUil
watt mmsFP H-J
SAMPLE BOX NUMBER
CLEAN-UP MAN_£Ll£_
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FLASK, FRONT HALF OF FILTER HOLDER
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FILTER NUMBER
IT-
/. V
CONTAINER.
CONTAINER ,
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WRINGERS. CONNECTORS, AND BACK '
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_m|
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MOISTURE
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NET VOLUME
S1UCAGEL
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NET WEIGHT
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TOTAL MOISTURE "Z.Z.S. /
B-78
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT
DATE
SAMPLING LOCATION.
SAMPLE TYPE ^M«
RUN NUMBER -jfa.
SAMPLE SOX NUMBER
CLEAN-UP MAN
COWENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS),
FLASK. FRONT HALF OF FILTER HOLDER
LABORATORY RESULTS
FILTER NUMBER
*•.<.
CONTAINER*!!
CONTAINER .
."I
FRONT HALF SUBTOTAL.
BACK HALF
HPINCER CONTENTS AND WATER WASH OF
HPINGERS. CONNECTORS. AND BACK '
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERV CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER ,
BACK HALF SUBTOTAL
_»i
-»i
TOTAL
MOISTURE
•(PINCERS
FINAL VOLUME T~ f
INITIAL VOLUME
NET VOLUME
SIUCAGEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
TOTAL MOSTURE
B-79
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
1C -
DATE.
SAMPLING LOCATION .
SAMPLE TYPE .
RUN NUMBER.
l/-P7y.
SAMPLE BOX NUMBER
CLEAN -UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE IBYPAS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER .
LABORATORY RESULTS
"I
."I
FRONT HALF SUBTOTAL.
BACK HALF
IMPINGER CONTENTS AND WATER WASH OF
WRINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS, CONNECTORS,
AND BACK HALF OF FILTER HOLDER
MOISTURE
MPINGERS
FINAL VOLUME
INITIAL VOLUME ^-°^ •>
NET VOLUME -Lk-£ •<
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ETHER-CHLOROFORM
EXTRACTIQ"
CONTAINER
BACK HALF SUBTOTAL
TOTAL WEIGHT
m(
IT[
"•1
mi
TOTAL MOISTURE ) 1 7' 5 I
B-80
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT.
DATE_
SAMPLING LOCATION ^O^-i
SAMPLE TYPE "JMJ-'-<.--fc/i
RUN NUMBER C. ~.X
SAMPLE BOX NUMBER .
CLEAN UP HAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
"I
."I
FRONT HALF SUBTOTAL.
."I
BACK HALF
MPINCER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE »ASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
j"i
mi
TOTAL WEIGHT
MOISTURE
•PINCERS
FINAL VOLUME ±is »'
INITIAL tfQI IMF A".OO_ Hi
NET VOLUME '
SILICA GEL
FINAL WEIGHT *-37.>.
INITIAL WEIGHT ^~CT I
NET WEIGHT . VI i 5 . I
TOTAL MOISTURE 1 ~> 7'
B-81
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT
MTF
SAMPLING LOCATION ^ "" ^'€-/
SAMPLE TYPE /V^TT /^/"X^c/
RUN NUMBER d> ' 3
SAMPLE BOX NUMBER
CLEAN-UP HAN 6'^)
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS),
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER .
LABORATORY RESULTS
"I
FRONT HALF SUBTOTAL.
BACK HALF
MPINGER CONTENTS AND WATER WASH OF
•RINGERS, CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE •
•PINCERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
OUCACa
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
_»l
BACK HALF SUBTOTAL
mi
TOTAL HEIGHT
TOTAL MOISTURE
B-82
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT.
PATF 'I- I • V 3
SAMPLING LOCATION 5 ;<-.»
SAMPLE TYPE fa'7^c<4
RUN umiiBEB K - I
SAMPLE BOX NUMBER
CLEM-UP KAN _m c
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
BACK HALF
HPINCER CONTENTS AND WATER WASH OF
WPINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE »ASH OF IMP1NGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
COWENTS:
NET VOLUME
nucAca
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
CONTAINER iii__2#»< .
CONTAINER
FRONT HALF SUBTOTAL.
LABORATORY RESULTS
»C
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
-»i
-«n
-«l
TOTAL
TOTAL MOISTURE.
B-83
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
II
DATE.
SAMPLING LOCATION
SAMPLE TYPE
•UK NUMBER K '
SAMPLE BOX NUMBER
CLEAN-UP MAN ^MC
COMMENTS.
/~ /
FRONT HALF
ACETONE »ASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER .
LABORATORY RESULTS
"I
FRONT HALF SUBTOTAL.
BACK HALF
MPINCER CONTENTS AND WATER WASH OF
WRINGERS, CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF MIPINCERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
•PINCERS
FINAL VOLUME 2.
HITIAL VOLUME
NET VOLUME
SUCAGEL
FINAL niGHT ^-'.'
INITIAL WEIGHT
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
TOTAL WEIGHT
TOTAL MOISTURE 7. 60 .
B-84
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
DATE.
SAIPUBG LOCATION
K -
SA»LE BOX NUBBER
O1AR4JP •*«
./- /
COWDTTi
FRONT HALF
ACETONE »A» OF N0221.E. WBE. CfCLONE (8YPAS).
FLASK. FRONT HALF OF FILTER HOLOER
FILTER »l»BER -
LABORATORY ftESULTS
_ ,—"I
CONTAIREft .
FRONT HALF SUBTOTAL.
BACK HALF
•PIKER CONTENTS AND VATtR f ASH OF
•PINCERS, CONNECTORS. AND SACX '
HALF OF FILTER HOLOER
ACETONE W«H OF IMPINGE*! CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER.
ETHES-CMLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
TOTAL WEIGHT
MOISTURE
FOULVOLlflK
WTUL VOLUME ±=£2 - •*
NET VOLUK ^U - *
imruu. itiCHT
RETIEIGHT
B-85
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
rm
SAMPLING LOCATION $c'"
SAMPLE TYPE
RUN NUMBER.
hk»-,-)
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS.
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK, FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER*'
CONTAINER
FRONT HALF SUBTOTAL.
BACK HALF
IMPINGER CONTENTS AND WATER WUM OF
IMPINCERS. CONNECTORS. AND BACK '
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINCERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
CONTAINFR
BACK HALF SUBTOTAL
TOTAl WFIGHT
tnj
rl
mi
TI
MOISTURE
WRINGERS
FINAL VOLUME
INITIAL VOLUME ^--^ •!
NET VOLUME "m* - •!
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
TOTAL MCOTUHE
B-86
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
- V-S-3
DATE.
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
,t
LABORATORY RESULTS
FRONT HALF SUBTOTAL.
BACK HALF
IMPING ER CONTENTS AND WATER WASH OF
MPINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS, CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
F.XTRACTI01 . .
GOHTMNFR - ... .
BACK HALF SUBTOTAL
TOT*L K»FIGHT
mf
W|
"I
"t
MOISTURE
MPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
TOTAL MOISTURE
B-87
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
DATE.
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
L'~L~
SAMPLE BOX NUMBER
CLEAN UP «AN tW
COMMENTS-
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS). CONTAINER.
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER _^-g> • t'534,7 CONTAINER .
LABORATORY RESULTS
FRONT HALF SUBTOTAL.
BACK HALF
MPINCER CONTENTS AND WiTER WASH OF
WPINCERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGER1 CONNECTORS,
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
mi
TOTAL
MOISTURE
•PINCERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILJCA GEL
FINAL WEIGHT
INITIAL WEIGHT
MET WEIGHT
TOTAL BOISTURE
B-88
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
DATE.
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER L-~t—
SAMPLE BOX NUMBER
CLEAN-UP MAN
CtUHENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS). CONTAINER.
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER _£=£ _' ***> 3<>7 CONTAINER .
LABORATORY RESULTS
FRONT HALF SUBTOTAL.
BACK HALF
HPINGER CONTENTS AND VATER WASH OF
fltPINGERS. CONNECTORS. AND BACK *
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINCERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
_«t
mi
TOTAL
MOISTURE
•PINCERS
FINAL VOLUME J° $ •'
INITIAL VOLUME 2-"*-' •<
NET WEIGHT
TOTAL MOISTURE "Z.Z3.7
B-89
-------
TRW
EPA METHOD 5
ANALYTICAL DATA
PLANT
BATE
/- /- 8JS
SAMPLING LOCATION
SAMPLE TYPE /^Pa
RUN NUMBER £--3
SAMPLE BOX NUMBER
CLEAN-UP MAN_£Lf-
S'
COMMENTS:
OJ7tf7' /- Z-
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK, FRONT HALF OF FILTER HOLDER
FILTER NUMBER *2. 1~_
LABORATORY RESULTS
."I
FRONT HALF SUBTOTAL.
BACK HALF
WRINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK '
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
-"i
TOTAL WEIGHT
MOISTURE
MPINGERS
FINAL VOLUME j£L£_ »l
INITIAL VOLUME "**T «l
NET VOLUME
SILICA GEL
FINAL niGHT
INITIAL WEIGHT
TOTAL MOKTURE 7-
B-90
-------
APPENDIX B-5
SASS FIELD DATA SHEETS
-------
TRW
CNVIHONMtNlAL INGINCCRING DIVISION
DO
I
IO
ro
mi r mi lit*
^-f THE f-g>fr'l
__
MMM'IIC »««ll.«t '^, Vf ~~
milt tMIMM. t».l — y. IS " //«- tf
f. •» -t - c -
•j -S-i
nwf UMM M »• -•' - v
mmt 1.1. "-.. 'f* ^^^J
•*»-! HMWI »l*^»
5^s«;
11
H1)'
tt'7
Zi
in
Ail
jid
iic
_£i
1005
j^4
IOS5
IMP
r AtS"
'(?•». i 0
e>"7 4,
ioi4.q
a.
la
2,C
4.1
_L2_
•IfMUliMH
/.fe
16?
l<
A1)
JJLl
4^^
Dt
44'T
ii.
-JO
s?
To!!^
££-
-v
/7
C7
17
\±-
I1?
.(41
o
/12C
16/
4i5
Vx
44-
A2.
Jf3L
_©_
O
TIBMKI
O
o
• 04:
-------
CO
I
TRW
tmiHONMCHTAL CNGINCfRING DIVISION
S ^ rt i- £ Jt_
tnjr-
IMIMdtlM. «..„„.».„. _S_£5i_
Miur i.», Mu
M-l
.u 1
sr< nr
c -?
I'M
1155
174
f?CP.
125^3 4 10
1 ) ,<*&
24.
LU.
• IMCI M11IM1
bi"";'i!«
O-
LSe,
'•
5 1-
•TiT-
M.
12 O
-31
Joi
II ^
II"?
1£2Q^.
i
4^4-
5-5
S7
©
O
O
O
44.
44-1
-------
SASS AlttLTTICAL DATA
riant /, C
Sevpllng Location -^ .L
Recovered By/, ' -• -
Recovery Date/4; -
Sample Mo. ff- - S ~/
Rim Mo. ' -"
Run Dace_' -
Analyit Reeponalble CM
Calculaclone and Reporc Reviewed By V"
Report D«te i J.
FILTERS USED
U.td
(yti/no)
Pretared Con
(No.)
"V
IMPDiOER VOLUMES
InltUl
Final
•~» ^50 ,J)
Flrat '
Second
JUT
.* J .
TOTALS I 5e
•J.-J So
So mi
SILICA GEL WEIGHTS
Initial
Final
'/A 7/n
TOTAL GAIN / V 77- ? «U
B-94
-------
APPENDIX B-6
ANDERSEN PARTICLE SIZING FIELD DATA SHEET
-------
PARTICLE SIZING FIELD DATA
METHOD: ANDERSEN IMPACIOR
Jill.
tiL
CD
I
VO
FILTER NUMBERS
PRE-IMPACIOR ttf
SIAGE 0 JM
SIACE 1
SIAGE 2
SIAGE 3 .
STAGE 4 .
STAGE 5
STAGE t
STAGE 7
FINAL MLItt '110
SAMPLING LOCATION
SAMPLE Wl fite
RUN WMER [fl)
OPERATOR
AMIIENT TEMPERATURE JL£f£__
MROMEIRIC PRESSURE 7_S".7G
STATIC PRESSURE. (PJ
METER CORRECTION FACTOR
-'?, IS
PR06E LENGTH .S
NOZZLE I.D.
•' \
ASSUMED MOISTURE, 1
IHPACIOR
MEIER M>« NUH8ER _
MEIER *M 3.3L
C FACTOR /
(O
REFERENCE tp O~ff
READ AND RECORD ALL DATA Wi»
MINUTES
TRAVERSE
WIN!
«MU
CLOCK TIME
hr. CLOCK)
O
15'DO
GAS METER READING
IK) fP
in-
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
DESIRED ACTUAL
STACK
TEMPERATURE
(T).*F
OBY GAS MEIER
TEMPERATURE
OUTLET
(T. )'.
"out
PIMP
IACCUM.
ln.Hg
IMPACTOR
IEMP|RAIURE
IHPINGER
TEMPERATURE.
.£?
//ff
//a.
Is.
540
AOV).
.r
M
Sot. 3
-------
CO
VO
FILTER
PRE-IHPACTOR
STAGE 0
STAGE
STAGE
STAGE
STAGE
SIAUE
STAGE
STACt
2
3
4
5
e
r
-f_\.i
•n1
•in
M^j
-1 'i
'I %
L\"\
H"\
NUMBERS
4\
,
•1
;
t
I
1
ANDERSEN FIELD DATA
PLANT iml , i\uUlli., I.u-k
M1E 10 IZ-T 1X3
SAMPLING LOCATION
SAHPLE TYPE ¥<*-{ S'i^
•sun
-&tv-
DRY GAS METER
TEMPERATURE
INLET
It- )"F
•in
no
IO~J-
~^^,
16 •>
•05
OUTLET0
'•out
J04
10 I
$
• S
PUHP
IACCIM,
In. 1)9
^
-^
IHPACTOR
TENPgRAIURE
£QG«F
V&SL
45t-
^Rfj^
""'
<\£)
Quo
IMPINGE*
TEMPERATURE.
*»
"
-------
A-l
ANDERSEN FIELD DAM
DO
CO
JiiL
FILTER NUMBERS
PRE-IMPACTOR Hll
SIAGC 0
STAGE I
STAGE 2
STAGE 3
STAGE 4
STAGE 5
STAGE 6
••AGE 7
FIN*. rl
MtS
SAMPLING LOCATION
SAHPLE IVPE
RUN NUMBER 2 ' J
OPERATOR
' A'.///rtl//v
M1.H
iliLl_
Mtl
.TE3
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. J
NOZZIE 1.0. . I2.S
ASSUMIO MOISTURE. I /C>
IMPACTOR NUMBER ^/
METER BOI NUMBER S£ e-"
METER 6H y fjT
C FACTOR . 7 ^CL
REFERENCE 4P .5p
' ^*/f?
READ AND RECORD ALL DATA EVLRV / 5^ MINUTES
IRAVERSE
>OINT
UfiER
C'l
A-V
CLOCK TIME
^424 dr. CLOCK)
SAWtlSfr-^.
TIME.aln. ^~^
O
l<
/<
30
|Oo-7
/^i
/o3k
;r.
r J.8
ry 4^j-^
^
ORIFICE PRESSURE
OIFFEKENTIAL
(lH).ln.H20)
DESIRED
.£-?
.a«»
,t
ACTUAL
.17
'<"?
!>
STACK
TEMPERATURE
-------
fi'
*
L,
FILTER NUMBERS
PRE-IMPACTOR /|%')
STAGED
STAGE 1
STAGE 2
STAGE 3
STAGE 4
STAGE 5
STAGE 6
STAGE 7 H
FINAL FILTER
Vn _
DATE _
SAMPLING LOCATION Ink t A
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPfRATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (PS) —
METER CORRECTION FACTOR
PROBE LENGTH
NOZZLE I.D. _
ASSUMED MOISTURE, t
IMPACTOR NUMBER jt|
METER BOX NUMBER
METER AH ^
C FACTOR ^
REFERENCE »p £
./70
READ AND RECORD ALL DATA EVER*
MINUTES
TRAVERSE
'DINT
NUMBER
A -F
c-R
CLOCK TIME
•^M hr. CLOCK)
SAwTTSfr^^
TIME ..In. ^^
O
r*
?6
/JTS"
n/&
/ja«r
GAS METER READING
(V.) ft?
v<«
SV7.V&V
/.T^.c>5
/frs.wr
//, **>i~
VELOC1TV
HEAD
(iPjl.ln.HjO
f\Q^*T~
,i\^r
ORIFICE PRESSURE
DIFFERENTIAL
(iH).ln.H20)
DESIRED
.IV
^
.4
ACTUAL
,3?
-.
IACCUM.
In. Kg
3
1
IMPACTOR
TEMPERATURE
.77-2.
V7<3
^b^
t<65
IMPINGER
TEMPERATURE.
6V
^
-------
o
o
FILTER NUMBERS
PRE-IMPACTOR 501
STAGE 0 SVt
STAGE I '.StTI
STAGE i
STAGE 3
STAGE 4
STAGE S
SIAGE 6
STAGE 7
FINAL FILTER
ANDERSEN FIELD MIA
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMB
OPERATOR
AMBIENT TEMPERATURE
BARCHETRIC PRESSURE o? "f, t> %
STATIC PRESSURE.
METER CORRECTION FACTOR /QOP
_ _
ft Z-'"^-
•EAO AND RECORD ALL DATA EVERY
PR08E lENGIII jr .S J
NOZZLE ID.
ASSUMED MOISTURE. I
IHPACIOft NUMBER '/
METER BOX NUMBER
METER »H
C FACTOR _/±
REFERENCE Ap
HINUTES
IRAVERSt
'OUT
UKBER
-^
rfK'-r'
CLOCK TIME
^JM dr. ClOCKl
SAHPLlSfi^vjSJ^
TIHE.Bln. ^^^
^
/5"
J^>
^0
/jjs-
/5"So
GAS METER ttAOINC
(».) fP
/^(T,/^
/bT»-i
/^r».^
ORIFICE PRESSURE
DirFEKEfTIAL
(«H).ln,H?0)
DESIRED
.21
.U.
.1'
ACTUAL
rffW
t*<°
fS
STACK
TEHCERAIURE
(TjA
'ffS?
^v
-------
3,2-
CD
I
ANDERSEN FIELD DATA
FILTER NUMBERS PLANT f-nW f>Y, V. \|, t.L.h,.
PRE-IHPACTOR •>)'! DATE 1
STAGE 0
STAGE 1
STAGE 2
STAGE 3
STAGE 4
STAGE S
STAGE 6
STAGE 7
j - j .'
' ^ 7
•> ,/^y
i"?. '
!» /CN/a?,/^
SAMPLING LOCATION .Tr-McA (K}
SAMPLE TYPE ^\h
j.' "
RUN NUMBER "^
OPERAT
JR&FMIC >(V/l-| (^Od1-!
J.?'^ AMBIENT TEMPERATURE ' At"° 1^
.•^l
•v XI,
^ 7f
BAROMETRIC PRESSURE 9^.^
STATIC PRESSURE.
METER CORRECTION
(PJl-^./s"/^.
FACTOR /.^>OS 3
PROBE
LENGTH 5 '5^
NOIRE I.D. ,/7S
ASSUMED MOISTURE, X
IHPACTOR NUMBER
METER
METER
/c>
/
B0« NUMBER V~t (~-
at 2.1<~
C FACTOR /22 /, y
REFERENCE 4P 3.1
0
FIHAL FILTER ff')i>
TRAVERSE
'01NT
NUMBER
C-8
ft-?
READ
CLOCK TIME
->-4Z4 hr. CLOCK)
TIME.nln.^^^
O
IS
36
/7J7
/7V-Z
/7^
GAS METER READING
(».) fl.
TWrTTtf
/^^. 7-7
/o^5->'
AND RECORD ALL
VELOCITY
HEAD
VA^3-
'^'l-*'^
DATA EVERY / S MINUTES
ORIFICE PRESSURE
OIFFEKENTIAL
DESIRED
.^9
.«!<-/
,
ACTUAL
£3
• ^
M^f
STACK
TEMPERATURE
^?-2» /
^t^^^^*~
-------
o, v
CD
I
o
fO
ANDERSEN FIELD DATA
i .16,
fllUa NUMBERS
OR:-IMPACTOR ';jN
STAGE 0 *ll%
STA^E 1 H ¥)
STAGE 2
STAGE 3
CTAGE 4
STAGE 5
STAGE 6
STAGE 1
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR f\ g/
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$) ^
METER CORRECTION FACTOR
FINAL FILTER ')
READ AND RECORD ALL DATA EVERY
MINUTES
PROBE LENGTH / C
NOZZLE
1.0.
ASSUMED MOISTURE. «
IMPACTOR NUMBER ^i.
METER BOK NUMBER /
METER »H / . V / _
C FACTOR . 99 'S
REFERENCE tp /IS
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NUMBER
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(aH),(n.H20)
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TEMPERATURE.
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FILTER NUMBERS
m-lHPACTOR t)'lt
STAGE 0
STAGE 1
STAGE Z
STAGE 3
STAGE 4
STAGE S
STAGE 6
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PLANT jjrO Cj Vj)tfcU\k(
DATE /t)/a~) IT 3
SAMPLING LOCATION Q- I
SAMPLE TYPE 4 * £to«a
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C FACTOR
REFERENCE Ap
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MKBER
a-9
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(ACCUM.
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5
-------
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I
I—'
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ANDERSEN FIELD DATA
PLANT Ffll£, Pt)C(v4 jJdfl.hu
DATE /Q /O^Tli'S
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SAMPLE T»PE
RUN NUHBER
OPERATOR fl.
AMBIENT TEMPERATUUE
BAROMETRIC PRESSURE
STATIC PRESSURE. (PJ
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PROBE LENGTH A> \ ft
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IMPACTOM NUMBER
METER BOI NUMBER
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At>0.
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STAGE 4
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PLANT ffll
DATE
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SAI1PLE TYPE R*i jCt tf
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HL
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431:
OPERATOR (XJ
AMBIENT TEMPERATURE _
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STATIC PRESSURE. (PS) —f
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MINUTES
PROBE LENGTH
NOZZLE I.D. .l^t*
ASSUMED MOISTURE, 1
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METER BOX NUMBER _J
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AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P^ -_
METER CORRECTION FACTOR
READ AND RECORD ALL DATA EVERY
MINUTES
P.108E LENGTH /£
NOZZLE 1.0. J/l(. ''
ASSUMED MOISTURE. I
IMPACIOR NUMBER
METER BOI NUMBER
ICIER M
C FACTOR
REFERENCE up
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TEKPJRAIURE
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560
-------
ANDERSEN riUD DATA
CD
I—»
O
PRE-IM
STAGE 1
STAGE
STAGE
STAGE
STAGE
SIAGE
STAGE
STAGE
FINAL
FILTER NUMBERS
ACTOR 5(/VS
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IMPACTOR NUMBER
METER BOX MJHBER _^
METER ill I *T|
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REFERENCE «t>
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METER CORRCCTION FACTOR
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POINT
UKBER
r\-f
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-------
PARTICLE SIZING FIELD DATA
METHOD: ANDERSEN IHPACtOB
O
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FILTER NUMBERS
PRE-IMPACTOR ^J ff I
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BAROMETRIC PRESSURE ~lf>. J5
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(M .
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METHOD: AljpERSEJi "IhPACTOR £
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. ^%. ^ I ' '
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IRAVERSE
'01 NT
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-------
PARTICLE SUING FIELD MIA
METHOD: ANDERSEN IHPACTOR
00
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FILTER NUMBERS
PRE-IMPACIOR S9 1
STAGE 0 31,3)
SIASC I 319
STAGC !
STAGC ,
STAGE '
STAG"! (
STAGC I
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FINAL flLt'R
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PROBE
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IMPACIOR NUMBER ff /
METER Ml NUMBER
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C FACTOR
STATIC PRESSURE. (Pt) -f
HfTER CORRECTION EACTOR
READ AND RECORD All DATA CVERt
MINUTES
TRAVCRSE
POINT
0
GAS HEIO1 READIND
<».) ft.
niocirr
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
UH).ln.H2n)
DESIRED ACTUAL
STACI
TEHPERATtmc
(T,).4F
wn GAS WIER
TEMPERATURE
OUTLET
(T. )°
PUMP
lAccm,
In.Hg
IMF-ACTOR
TENP^RAI'JIE
WINGER
TEMPERATURE.
/70
Hifl
Jo
n*-
d2-
Ak
Mo-
-------
FILTER NUMBERS
PRE-IHPACTOR .
STAGE o :
StAGE 1
STAGE ?': •,;
STAGE 3 •„ .
STAGE 4
STAGE S -w
STAGE t _
. STAGE 1
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59*
'£
NOZZLE I.D. *i*~
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DS
t-i-
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AMBIENT TEMPERATURE ~lO °f
I/WOMETRIC PRESSURE 25 (e4-
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-------
c•(_-/
DO
I
FIIUR NUMBERS ' N.MIT
PRE-IMPACTOR S'JQ . . WTE
SIAGE 0
SIAGE 1
N FIELD OA1A
F/liC - f*poite/|o
/(^J//S^3
• 5 ? S SAMPLING LOCATION O' &~l.lff~— 1 • 'i
51 f
STAGE ? 5 9 t '
SIAGE 3 S '£ 5
STAGE 4 S?W
SWF * 5 "^ ,) • l
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SIAGE 7 ft « 1
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TIME . Bin. /^J-^
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AMBIENT TEMPLRAlURE ' ^ ~
lltl c2,J
^^ .
-
.5 S^
,T^
v-
-------
FILTER NUMBERS
PRE-IHPACTOR S
STAGE 0 2
STAGE 1
STAGE 2
STAGE 3
STAGE 4
STAGE 5
STAGE f
STAGE 7
FINAL FILTER
ftJLi~~i f\
T5T
SS'V
ANDERSEN FIELD DATA
PLANT pff\G.~
DATE so I;} <$ Il^>
GAS METER READING
(».) fl.
fcJrt.S74
t1«.^J?^>
-!)i*
STACK
TEMPERATURE
(T,).*F
DRV QAS HETER
TEMPERATURE
INLET
\r
/°r
ts<
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OUTLET
(T )°l
•out
/<>r
/«> >
s
PIMP
Mccin.
In.Hg
/C
/ 1.6
IMPACTOR
TEMPERATURE
'i,vy-r
'VjJ-p
fV7
IMPINGER
TEMPERATURE.
t>U
^c. .
-------
I
fr—•
I—t
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FILTER NUMBERS
PRE-IMPACTOR -
^_^
DRY GAS METER
TEMPERATURE
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OUTLET
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k^
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FWf
»ACCIN.
In.Hg
^-
^N
IMPACTOR
TEMT^RATURE
T 1-io"
IMI'INGCR
TEMPERATURE.
\
\
\,
\
\
-------
PARTICLE SIZING FIELD OA1A
METHOD: ANDERSEN INPACTM
CD
I
FILTER
PRE-IMPACTOR
NUMBERS
STAGE 0 S C,$
STAGE 1
STAGE 2
STAGE }
S<,V
Stf,
Sfef
STAGE 4 5 (.
READ AND RECORD ALL DATA EVER*
MINUTES
IRA»ERSE
•OINT
OVER
\^
CLOCK TINE
•"M" •»• 0.«M
SAMPliilB^^
TINE .Bin. ^^»^
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\
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GAS METER REMIND
«».) »P
1 \
\. t°
^\
VELOCITY
HEAD
UP^.U.HjO
/L
rV
ORIFICE PRESSURE
DIFFERENTIAL
(»H).)B.HjO)
DESIRED
v
*^
ACTUAL
\
<-
STACK
TEMPERATURE
(I,). F
\^
\^
Wt GAS METER
TEMPERATURE
INLET
IT. ?F
"in
\^
OUTLET
(T. )°l
•out
K^
~^-^
PUV
IACCUI,
U.H»
IMP ACTOR
TEMP|RAIURE
IHPINGER
TEMPE1AIUIE.
-------
APPENDIX B-7
PROCESS SAMPLE DATA SHEETS
B-116
-------
SOLIDS FIELD DATA
GENERAL
SimpJoSto
TypoofSottico _
Sompflni Lootioo
Simpb Typo:
CilcuUtion wid Report Rtvi«M*d by:
- n
Rtport DM
S.mplin, Dc,.-
Compoott Simplr Y«
or No
s«npto Mn or Vd.m.
If Compoutt, Numbtr ind/or Volnim of Portiow of Composto:
Stmpto Oncription: HomogtMoos _ Httorefonooas
Urft Ho cot _ Color _
brnplii* Problem t
Powdor
Siwlt
Hoots
Dry
ScccP
B-117
-------
StmettStt
SOLIDS FIELD DATA
GENERAL
Sompfinj Oovico -^l&ftr <- .1>Of CO Sunpk Mm o, Volamo
Compost! Simpto: Y« X. or No .
If Compofitf, Namtaor ind/or Voluim of Portion of Compofte:
Simpl* DtKriptioa: HomogtMous Httorofonooiu . Powdor _
Urffi HOCB CotoT _ W« _ Dry
Simplini Profaloms ,
SmtH
10
B-118
-------
SunpbStr
LIQUIDS FIELD DATA
GENERAL
>u
, Typ»«f Sown',
* SimpkTypt: Aqatoui T ^ Suny..
' Simpto Numibrr P|^C.-
-------
LIQUIDS FIELD DATA
GENERAL
SampbSta
Typa of Sourct ilW^'i-Vf
J^>U
Simpling Location
Sampta Typi: Aquaous
Sampta Numbtr
Sorry
C*leuUtionj and Riport Rtvitwtd By
Orpok
Ripert Dm
Sampla Mas or Vofama
Compoth* Simple: YM
trNt
If Composin, Numbtr and/or Voluma of Portions of Cwnposita:
Sampta Dascription: Fluid Viscous Hot _X.
Homooanaous * Hatarooanaoui
Sampling Preblams
COM.
Frowiag
Still
Color
B-120
-------
SOLIDS FIELD DATA
GENERAL
•™~
-------
SOLIDS FIELD DATA
GENERAL
SempieStf
Cikuljtiora tnd Report Rninw^ by
Otviei
or No
Caapttitt Simpta: Y«
If Compotitt, Number and/or Volume of Portions of Composite
Simple Description: Homogeneon - , Heteroteneous
Urge Ptocoi - Color -
Powder
Smefl
Piecot
Wtt
Dry
ms
B-122
-------
LIQUIDS FIELD DATA
GENERAL
Samplt Typi: Aqatoui
Simpl. NumhM t W C -
^Vi5
Analyf* Rttpnnuhb . V_ViJ
y
f- -;
P/££.
Calculationi and Rtport Rtvwwtd By
i'' L~-I 3-> Jie.u_,Wc^--) \
- ^^ tt>0 ^"Nrrn fV^^ii]
^*3^ ^ \ 6 J
Shiny Or|»ie
^- D>MT«kM /^'-W
RF r---
/ A "'"'• <•"' / '"
N / /*• R^iart D«M ' * - t , ^-.."=5
s*mplt M«n or Vohimt
Compotit* Sampto: Yn
trNa
If Compotita, Numbar and/or Volumt of Portioiu of Composita: —
Sampto Otscription: Fluid ^ Voceyi Hot _
Homovanaous Hataro«anaous
Sampling Preblams
Cold.
Flowing
Color
\\<-
Still
or
B-123
-------
LIQUIDS FIELD DATA
GENERAL
Simple She
Type of
Samplrna,
Sample Type: Aa.oeouYI..^ Slurry Orpiic
Sample Number fjvu- ± -e
Analyst I
Cdculitiont and Report Rtvwwwl By Rtpon Dtt»
I Device __i^UC^i£th: Sample Mas or Votoma
Composite Sample: Yes *^*^ or No .
^-^ ~^
If CompOHtt. Number and/or Voluree of Portioni of Composite: Oc^U^ /
Samph Description: Fluid Vbeoai Hot __!^_ Cold Flowiif —i^_ S«
Homootntous Heterogeneous Color
Sampling Problemi ^
4
B-124
-------
SOLIDS FIELD DATA
GENERAL
SnMi*i imtiw
timh Type. Infinfc £ IkiMfc
"-iCrO_-3 O«T*
Ciloilnwm mJ Rtpwt Rtmnd ly: ^~ '"' ""**11 D*1*
V«_
H C«m».rt, fombtr ud/br VobM g| PoctiM if CMpwtr U^ |O •»-*-> /
SiiMto Dncnpti«: Horn Ihauiumi Pmto SM| Am
LMpHMi Mw «•• * Ort
Snapliai fraklmi
B-125
-------
SOLIDS FIELD DATA
GENERAL
lMi«uk <
«». P/MC -£'
AiMlyn RiMMiiiU
blolniom »t RDMR Rnmml by:
|" ^ ^a^ng^&j— . _
: to fT _ 522. Bi»«rt DM JAN
Compmi Simple Y«i L. m H» .
II Canyoiiti, Nonbtr urt/or Voluim if PmtlMi «* Ummit*
SinilUt Oncriptwi: Htmmumi llimu|n«iui
Dry
— 2. SAW-I- ScooP±>
B-126
-------
LIQUIDS FIELD DATA
GENERAL
Si me* Shi
TypofSmet _L
Simpint Location
Aqonui
OrpM _
OntllkM
UaMnn Md Rtptn RtnmW By
«i 1AM
vJ ^ j i
Cmponn Smith:
Yn
If C*m»«iti, Nimbv lad/Of Vohim. of NctiMn •) C*»p«rt>:
ctiirtill: FliU _^ — Vfenn - H«t
Simplwi Fnttomi
COM.
SUP .
3\"1& :
/64f
/~7^r
' &<$-
i^^r
B-127
-------
LIQUIDS FIELD DATA
GENERAL
fc-&i
wiplt: Y«
If Cm*MB. Nnbw iid/tr Vol«M ri tottan if C**f«iti:
SM^II Dtxnpue* FhU Vac«n Hit
Swfto Mn w VifaiM
"Bg.1^
SW.
*^£J^_^j^S.
^f
-(-
4
^
B-128
-------
SOLIDS FIELD DATA
GENERAL
(L
io* «4 Rtpon MnitiM^ ly:
tflfj
II Com»«Bn, Itambif u*Mr Votaim
BJL
Dry
B-129
-------
SOUOS FIELD DATA
GENERAL
Sunptnt LottM
J8£
Coiwnin bn»lr V« - « •• - .
It C*m*eHH, NiKbu ii>
-------
LIQUIDS FIELD DATA
GENERAL
^Jf ,s,
S«m»l»T»n: AqiMn —£__ _ 9urv Oipiil
DM Trim
UoiMwn «^ Rtf*n Rnaiirt l»
C r '
n-- -~~\~rtlJL>-~ SMDHItai^VlliM
Nmbtr ••
-------
LIQUIDS FIELD DATA
GENERAL
Tyurf
!• (Vital UatiM
iHcO.te 6*k r^J2r.
If Cwnfrtn, MMkn I*/M Vokim »lin:
Svn*
-------
SOLIDS FIELD DATA
GENERAL
_ S
(tan T«l
: H / A"
II Cin^ran, N.«taT wd/gr Vetam •( Nnlwi •< Ci»»ah«:
Dry
B-133
-------
SOLIDS FIELD DATA
GENERAL
t-i lta.T.ta. /'I /'"'/'
SM)«tN«»*«r
blnldMrn wd Ri»«n town* »»: " _ R«**it DM
J ft r
C*m*ntt Sm*te ¥• - • N*
If C»mHirti. NymkH in«fer Vrtim
{•••to Dncnptiu: mimjmoii llinn|ii»y|
UtfiFlMM Crt« Wn , Dry
Sm«te| Praklmt _
4-
B-134
-------
APPENDIX C
SAMPLING AND ANALYTICAL PROCEDURES
-------
APPENDIX C-l
DETAILED SASS OPERATING PROCEDURES
(ORP PROGRAM MODIFICATION)
#2
-------
DETAILED SASS OPERATING PROCEDURES
(ORP PROGRAM MODIFICATION)
The acquisition of the sample for the ORP test program using a SASS
train will generally require two, and in some cases, three persons for
equipment assembly and disassembly. After assembly, the train requires
one full-time and one half-time person for operation. The remaining
manpower is then available for other on-site efforts. Each SASS train
run will consist of approximately a 5-hour period. The number of required
personnel for this function will not increase regardless of the number
of sample sites, provided that a sufficient time allotment exists within
the sampling task to allow for consecutive sampling. Manpower projections
can thus be determined by considering the number of SASS particulate
samples required to characterize the location in question, the time
required for the acquisition of each sample, and the number of personnel
and/or samplers available for the task.
i.l EQUIPMENT PREPARATION FOR SAMPLE COLLECTION
The following appendix discusses the equipment preparation required
for the SASS train, including procedures for cleaning the train components
and sample containers. For further information on the device, see the
Operating and Service Manual Source Assessment Sampling System. The
SASS train schematic and other parts of the train are shown in Figure 3-3.
The first stage in preparing a new sampling train and new sample
containers for sample collection is prepassivation with a nitric acid
solution. All metal and glass surfaces in the sampling train that come
in contact with the sample will be prepassivated by a 30-min standing
contact with 15 percent (v/v) aqueous nitric acid. Use a stiff nylon
brush or hard Teflon scraper to aid in cleaning encrusted materials from
the surfaces if necessary. Agitate the parts initially to remove trapped
C-3
-------
air bubbles. Rinse in a second solution of 15 percent (v/v) HN03) then
rinse with distilled water. Next, rerinse by spraying thoroughly with
alcohol (taking care to cover all surfaces) or dip in alcohol and agitate
for 10 seconds. Finally, dry with purified air or nitrogen. If the
impingers are to be used immediately after cleaning, they should be
thoroughly dried or rerinsed with distilled water to prevent foaming
when the peroxide is added.
A different approach is used for subsequent cleanings of SASS train
components and for bottles holding impinger solutions for the ORP test
program. The components and receptacles are cleaned in three successive
stages using a different solvent in each stage. The solvents are hot
soapy water, distilled water, and acetone in the order listed. This
will remove all extraneous particulate matter and produce a clean, dry
surface. A contaminated train component may not be used in a sampling
run. All equipment treated in the above fashion must be placed in a
clean area to await the next test. The bottles holding the impinger
solutions are cleaned with distilled water.
The field area in which these cleaning operations are performed
must be as clean as possible under existing field conditions. An enclosed
space is required in which reasonable precaution has been taken to
remove spurious dust, dirt, or particulate contaminants. Reasonable
precaution is intended to mean that the area has been swept clean, doors
or significant draft-inducing sources have been closed, and all work
bench areas have been wiped down.
1.2 APPARATUS CHECKOUT - SASS TRAIN
The following tasks will be performed in the home base laboratory
prior to shipment:
a. Assemble all components required for the complete system.
b. Clean components in accordance with the procedures described
in reference manual.
c. Obtain a sufficient quantity of solvents to maintain adequate
reserves during the elapsed time in the field.
d. Obtain a tank of purified dry nitrogen or clean compressed
air.
e. Accumulate an inventory of Swage!ok fittings (in triplicate)
for each SASS train.
f. Examine all SASS train parts closely for defects that might
induce down-time problems in the field.
C-4
-------
g. Leak-check the entire system.
Besides the cleaning procedures, leak-checking the train prior to
field use is one of the most important pretest tasks to be performed.
This procedure can save hours of time in the field. The leak-checking
procedure involves assembling the entire train, sealing the probe tip,
opening the isolation ball valve, turning on the pumping system, and
observing flow meter gauges for the existence of any appreciable flow.
Evacuate the train to 127 mm Hg (5 in Hg). The allowable leak rate for
the SASS train is 0.0014 nrVmin (0.05 ftVmin) at this pressure. Close
the isolation ball valve and leak check the remainder of the train at
508 mm Hg (20 in Hg). The leak rate should again be less than
0.0014 m3/min (0.05 ftVmin). If this criterion is not easily achievable
using Teflon gaskets in the system, Viton A gasket substitution may
facilitate meeting this standard. The instructions accompanying the
train will present in detail the steps involved in leak-checking the
system.
1.3 SASS TRAIN SAMPLING PROCEDURE
The SASS sample is normally acquired at a point of average velocity
near the center of the duct (the average velocity being determined by a
velocity traverse). During the ORP test program the sample will be
drawn from multiple points. Sample point location will be determined
either by EPA Method 1 specifications or the Inhalable Particulate (IP)
protocol depending on velocity stratification, access and sample time.
The sample will be withdrawn at a constant flow rate using a nozzle that
is specifically selected for near isokinetic conditions (±20%) when the
test is initiated. Nozzle selection will be determined from preliminary
measurements at each location.
The steps involved in using the train to acquire this sample are
described in detail in the manuals provided with the SASS train. An
outline of the procedure follows:
I. Test Site
A. Prepare sampling port on duct, flue, or stack.
B. Secure electrical power.
C-5
-------
II. SASS Train Assembly
A. Attach probe to oven.
B. Place the three cyclones and filter assembly in the oven
and connect the 10 pro cyclone to the probe. (Note that
to achieve the proper size fractionation, the vortex
breakers for the ">10 urn" and for the "10- to 3-um"
cyclones should not be used.)
C. Assemble impinger train.
1. Fill impinger bottles with the reagents listed in
Table B-l.
2. Place the impingers in the tray in impinger case,
cap bottles, and make appropriate connections.
3. Fill impinger case with ice and water.
0. Connect oven outlet (i.e., filter housing outlet) to the
first impinger.
E. Connect vacuum pumps (in parallel) to the last impinger
outlet.
F. Connect all temperature sensors and power lines to control
unit.
III. Checkout and Inspection
A. Run gas flow leak check.
B. Check temperature indicators with all thermocouples at
ambient temperature.
C. Heat oven and probe to 204°C (400°F).
D. Note operation of vacuum pumps and gas meter.
E. Inspect pi tot tube; also, compare results of volume
measured with orifice meter and dry gas meter. Calibrate
each as necessary.
IV. Operation
A. Measure stack temperature, moisture content, and velocity
profile.
B. Calculate size of probe nozzle needed for isokinetic
sampling and select and attach appropriate size nozzle.
The stack temperature and effluent water vapor content
must be considered when choosing the proper nozzle size
(preliminary measurement).
C-6
-------
Table 1-1. SASS TRAIN IMPINGER SYSTEM REAGENTS
o
I
Impinger
#1
#2
#3
#4
#5
Reagents
Nitric acid
(.1M HN03)
Nitric acid
(.1H HN03)
NAOH
Empty
Silica gel
Quantity
500 ml
500 ml
500 ml
Empty
750 grams
Purpose
Condense moisture
and radiochemical
metals
Condense moisture
and radiochemical
metals
Buffer acid/remove
S02
Prevent carryover
Condense moisture
and protect pump/
dry gas meter
-------
C. Calculate train gauge reading to achieve train flow rate
of 0.133 snrVmin (4.0 sftVmin). (This flow rate is
necessary for proper operation of the cyclones.)
D. Install probe in stream at desired point and turn on
vacuum pumps; adjust train flow rate to 0.113 sm3/min.
E. Collect sample. Monitor all temperatures and flow rates,
and adjust as necessary.
V. Shutdown
A. Close valves at pumps.
B. Remove the sampling nozzle train from inside the stack.
C. Turn off pumps.
D. Switch off main power.
Replacement of a clogged filter is a time-consuming process that
could require as much as 2 hours, depending on the sampling location and
the possible difficulties that might be encountered in removing the
housing. Once removed, the housing should be carried intact to a clean
area for filter removal. A second, preloaded filter housing should be
available for use when the first housing is removed for unloading,
cleaning, and reloading. Check this assembled replacement filter assembly
for leaks before placing it in service, then make a final check of the
pressure drop of the whole SASS system when the unit is again reassembled.
The 1-um cyclone reservoir should be checked for remaining capacity
whenever the filter is replaced. Take care not to contaminate the
contents during this inspection.
1.4 SAMPLE HANDLING AND SHIPMENT
A modular approach will expedite the explanation of the procedures
involved in sample transfer and handling. For this reason, the SASS
train is considered in terms of the following sections:
a. Nozzle and probe
b. Cyclone system interconnect tubing
c. Cyclones
d. Filter
e. Impingers
At the conclusion of the sampling run, the train is disassembled
and transported to the mobile lab unit or prepared work area as follows:
C-S
-------
a. Open the cyclone oven to expedite cooling, disconnect the
probe, and cap off both ends.
b. Disconnect the line joining the cyclone oven to impinger
assembly at the exit side of the filter and cap off (1) the
entrance to the 10-(jm cyclone, (2) the filter holder exit, and
(3) the entrance to the joining line, which was disconnected
from the filter holder exit point.
c. Disconnect the line joining the adsorbent module to the impinger
system at the point where it exits the adsorbent module. Cap
off the joining line and the entrance line to the impinger
system.
d. Disconnect the line leaving the silica gel impinger at its
exit point and cap off the impinger exit. Discard ice and
water from the impinger box to facilitate carrying.
At the completion of all sample transfer activities, all SASS train
components must be completely recleaned in preparation for the sampling
run. This may be accomplished by following the steps outlined.
1.5 SASS SAMPLE RECOVERY
Figure 1-1 is a flowchart of the sample handling for those SASS
fractions containing particulate matter. Each aluminum foil packet with
the individual cyclone catches will be dessicated and weighed separately.
The acetone rinses for all stages will be combined and evaporated to
dryness, dessicated and weighed. The four (4) individual stage weights
will be summed with the combined acetone evaporate and totaled for the
total mass particulate determination.
Figure 1-2 is a flowchart of the sample handling for the impinger
contents. The impinger catch will be used to determine moisture and
condensed radiochemical metals. Possible analysis of metal content and
associated radionuclides may be performed on the impinger contents. A
buffering solution of sodium hydroxide (NAOH) will be used in the third
impinger to prevent acid carryover and aid in protecting the pump/dry
gas meter assembly from corrosion. An empty fourth impinger has been
added to ensure adequate condensation of moisture from the sample stream.
The fifth impinger will contain silica gel.
C-9
-------
n
"Probe and
Noiile
o
I
Filter
Housing
Acetone Rinse
(Brush as necessary)
IK
Add to I0n (./.lone Hinse.
Step 1: Tap and brush content!
froai walls and vane Into lower
cup receptacle.
-(
Step 2: Reconnect lower cup receptacle
and rinse adhered wterlal on walls and
vane Into cup with acetone.
Step 1: Tap and brush contents froai
wells Into lower cup receptacle.
Step 2: Reconnect lower cup receptacle
and rinse cyclone walls and Interconnect-
ing tubing with acetone Into cup.
Step 1: Tap and brush contents fro*
wells Into lower cup receptacle.
Step 2: Reconnect lower cup receptacle
and rinse cyclone wells and Interconnect-
ing tubing with acetone Into cup.
Step 1: Reaove filter, roll, and place
In tight sealing, petrl dish.
Step 2: Brush partlculate fro> both
housing halves Into filter container
and seal.
Step 3: Rinse adhering partlculates
fro* !„ • cyclone tubing and front
half of the filter housing Into the
combined rinse using acetone.
Reoove lower cup receptacle
and transfer contents Into
a tared aluerinun foil pocket.
Reenve lower cup receptacle
and transfer contents using
acetone.
Kl
Rnuve lower cup receptacle
and transfer contents Into
tared almlnua foil pocket.
Remove lower cup receptacle
and transfer, using acetone.
ftenove lower cup receptacle
and transfer contents
tared aluminum foil picket
Reoove lower cup receptacle
and transfer contents using
acetone.
NOTE:
Acetone - ACS
reagent grade
Ali*lnun foil
packets - prerlnse
wtfh acetone
Figure 1-1. Sample handling and transfer - nozzle, probe, cyclones, and filter.
-------
§
Implnger No. 1
Measure Volume
Implnger No. 2
Measure Volume
Implnger No. 3
Measure Volume
Implnger No. 4
Measure Volume
Implnger No. 5
Rinse with Known Volume of Distilled II20
Rinse with Known Volume of Distilled H?0
Rinse with Known Volume of Distilled
Rinse with Known Volume of Distilled
Weigh and Discard or Regenerate
Add Rinse from Connecting Line
Lending from Cyclone Oven to
First Implnger
Transfer to Anfcer Glass Bottle
and Measure Total Volume
Combine
and
Retain
NOTE: Metal/Radlochenlcal Potential
Analysis by EPA/ORP
Combine
and
Retain
Figure 1-2. Sample handling and transfer - SASS impingers.
-------
APPENDIX C-?
GENERAL PROCEDURES FOR OPERATION
OF INERTIAL CASCADE IMPACTORS
-------
GENERAL PROCEDURES FOR OPERATION
OF INERTIAL CASCADE IMPACTORS
1. Principle and Applicability
1.1 Principle. An in-stack cascade impactor is used to collect
and inertially separate the stack gas particulate matter into size
fractions. The sample is collected isokinetically ±20% at 4 points
specified as the centroids of equal areas. The material collected in
each size fraction is quantified gravimetrically.
1.2 Applicability - These procedures are applicable to the operation
of commercially-available cascade impactors. Andersen Mark III impactors
are to be used for the tests described in this test plan.
2. Equipment
2.1 Sampling
2.1.1 Inertial Impactor with stainless steel collection
plates are commercially available.
2.1.2 Collection plate substrates - These are used to reduce
the tare weight of collection surface. This is desirable as plate
loadings are typically on the order of 10 milligrams or lower. Either
aluminum foil, stainless steel shim stock, or glass fiber filter material
may be used.
2.1.3 Nozzle - This is made of stainless steel with sharp
tapered edge.
2.1.4 Pump (leakfree).
2.1.5 Probe.
2.1.6 Sample line, connectors (flexible tubing).
2.1.7 Metering system - This consists of a vacuum gauge,
calibrated orifice, and manometer (0-10 in. H20). A predetermined
manometer reading is maintained to insure isokinetic sampling.
C-13
-------
2.1.8 Barometer - This is used to measure atmospheric pressure
to ±0.1 in. Hg.
2.1.9 Thermocouple - This is necessary for measuring stack
gas temperature and the outlet of the impactor temperature to avoid
condensation of moisture.
2.1.10 Condenser/Impinger - A condenser, or impinger with
silica gel, may be used to remove moisture from the sampled gas. This
allows measurement of sample gas volume on a consistent dry-basis.
2.1.11 Pitot tube, manometer - A Type-S tube is used to
measure stack gas velocity, before each test.
2.2 Analytical
2.2.1 Dessicator (portable). Drying of impactor substrates
minimizes errors in weight measurement which would result from adsorbed
moisture.
2.2.2 Tweezers, small brush - These are for the recovery of
sample substrates and particulate material.
3. Procedures
3.1 Impactor Selection
3.1.1 The main criterion for determining the sampling impactor
is the expected particulate concentration of the stack gas. Commercially-
available impactors can be classified into two general categories:
a) Low flow-rate impactors - less than 0.1 ACFM.
b) High flow-rate impactors - 0.1 to 0.75 ACFM.
The following criteria are used to determine the appropriate class
of impactor for the test:
1. The estimated mass loading of particulate less than 5 miqron
diameter is less than 0.2 gr/ACF - use high flow-rate impactor.
2. The estimated mass loading of particulate less than 5 micron
diameter is greater than 0.2 gr/ACF - use low flow-rate impactors.
3.1.2 Right-Angle Precutters are often necessary to prevent
the overloading of the first collection stage of the impactor. As a
general rule, pre-cyclones should always be used when sampling stack
gases prior to a control device inlet.
3.2 Sampling Location Selection
3.2.1 Ideal conditions specify the selection of a sampling
site that is, if possible, at least eight duct diameters upstream from
C-14
-------
any flow disturbance such as a bend, expansion, contraction, or visible
flame. For rectangular cross-sections, determine an equivalent diameter
from the following equation:
Equivalent diameter = 2 (Equation 1)
3.3 Preliminary Velocity Traverse - Prior to sampling, determine
the stack gas velocity according to the procedures of EPA Method 2.
3.4 Moisture Determination - Prior to sampling, determine the
stack gas moisture according to the procedures of EPA Method 4.
3.5 Molecular Weight Determination - Prior to sampling, determine
the stack gas molecular weight according to the procedures of EPA Method 3
or gas chromatography with thermal conductivity detection (GC/TC).
3.6 Preparation of Collection Plates
3.6.1 Substrates - Aluminum foil or filter substrates should
be used because of the high tare weight of the collection surfaces.
Substrates can be purchased from impactor manufacturers or can be
hand-made.
3.6.2 Taring Collection Substrates
3.6.2.1 Ungreased surfaces - Dessicate the substrates
until constant weight is maintained. Record tare weight to the nearest
0.1 mg.
Note: In some cases (especially when collection substrates are
large filters), weighing can be simplified by using aluminum foil to
form an envelope around the substrate. The envelope can be tared with
the substrate, marked to correspond to the substrate, and then used to
contain the substrate and sample after the test.
3.7 Determination of Impactor Operating Temperature.
3.7.1 Gas streams above 350°F and unsaturated gas streams are
sampled at gas stream temperature.
3.7.2 Saturated gas streams below 350°F are sampled at a
temperature above the dew point temperature.
3.8 Determination of Nozzle Size - Determine the gas velocity (V )
at the points to be sampled. Select a nozzle size which will yield a
sample rate Q within the acceptable operating range of the impactor.
C-15
-------
3.9 Determination of Sample Rate - After selecting the nozzle
size, use Equation 2 to convert the sample rate indicated to impactor
operating conditions. Determine whether or not this sample rate exceeds
the permissible maximum flow for the impactor.
Tr
Q! = ^N x T~ (Equation 2)
Where: Qj = Sample rate through impactor, ACFM
QN = Sample rate at nozzle; stack conditions ACFM
Tj = Impactor operating temperature, °R
T<- = Stack gas Temperature, °R
Note: If the sample rate exceeds the permissible value, choose the
next smallest nozzle, thus yielding a lower QN-
3.10 Sample Train Assembly - Carefully place the collection
substrates on the collection plates and assemble the impactor. Plug the
inlet to the impactor and perform a leak test. An acceptable leak rate
is less than .02 ft/min at a vacuum of 10 inches mercury.
3.11 Determination of Length of Test - The limiting factor in
determining the sample time required is the quantity of mass collected
on the stages. Sampling should be conducted for a period of time necessary
to maximize the mass collected without overloading any stage. The
maximum mass permitted on any stage is about 10 mg. Performing a
preliminary test with a post-test visual determination is usually the
only way to determine the optimum sampling time. If an estimate of the
mass concentration is known, is is possible to estimate the sample
period for the preliminary test.
3.12 Sampling
3.12.1 The operation of the impactor at stack temperature
requires the positioning of the impactor in the stack with the nozzle
facing upstream. Sampling may start when the impactor exit temperature
is within 10 degrees of the stack temperature.
3.12.2 Turn the nozzle into the flow, start the sample pump,
and adjust the flow to the isokinetic sample rate. Maintain this sample
rate for the duration of this test to keep the size distributions fixed -
even if the stack gas velocity changes. Record the data at the conclusion
of the sampling period, stop the pump, and turn the nozzle away from the
C-16
-------
direction of flow. Remove the impactor from the stack, being careful
not to bump it against the stack or port walls. The impactor should be
maintained in a vertical position after removal from the stack.
Note: Precautionary measures are required for gas streams with
high negative pressure for prevention of backflow throught the impactor.
The nozzle should be plugged during impactor pre-heating. The impactor
is subsequently removed from the stack, the nozzle unplugged, the sample
pump started, and the impactor placed in the stack (which initiates the
test period). The impactor is removed from the stack and the pump is
stopped at the conclusion of the test period.
3.12.3 The velocity of the gas stream at the sample point
should be measured before each test run.
3.13 Sample Recovery - Disconnect the impactor at the probe.
Clean off any loose particulate from the outside of the impactor.
Transport the impactor to a clean area for disassembly. Begin disassembly
when the cooled impactor can be safely handled.
Precollector Cleanup - Begin by removing the precollector. Use a
small clean brush to help remove the collected material from the
precollector into a tared piece of aluminum foil. All the material from
the impactor nozzle to the outlet of the precollector is included in
this catch.
First Stage Cleanup - Remove the first stage substrate carefully
with tweezers. All material between the cyclone outlet and inclusive of
the frontside of the second stage nozzle is included with material
collected on the first collection plate. Use a brush to remove any
material adhering to the impactor walls or to the backside of the first
stage nozzle.
Second Stage Cleanup - All material between and inclusive of the
backside of the second stage nozzle and the frontside of the third stage
nozzle is included with the material adhering to the second substrate.
Third Through Last Stage Cleanup - Follow the same procedures as
for the first and second stages.
Note: Aluminum foil "envelopes" are used to hold large glass fiber
filter substrates.
The foil is laid out and the filter substrates are placed on the
foil. Any loose material is brushed onto the foil. The foil containing
the filter and loose particulates can then be folded.
C-17
-------
3.14 Sample Analysis - Analyses of the samples are performed in
the field. The substrates are placed in a dessicator and dried to a
constant weight. The substrates and cyclone catch are weighed to the
nearest 0.1 UQ and the mass is recorded.
Note: Table C-2 is a recommended checklist for cascade impactor
use.
3.15 References
1. Federal Register, Volume 36, Number 247, Part II. December 23,
1971.
2. Gushing, K. M. , J. D. McCain, and W. B. Smith. "Particulate
Sizing Techniques for Control Device Evaluation."
EPA-650/2-74-102, 1974.
C-18
-------
RECOMMENDED CHECKLIST FOR PARTICLE SIZING IMPACTOR USE3
1. Preparing the impactor train
a. Wash the impactor and pre-collector using an ultrasonic
cleaner if available.
b. Visually check cleanliness in good lighting. Jets must be
clear and sidewalls clean.
c. Obtain weighed substrates and assemble impactor.
2. Sampling
a. Assemble the impactor train and heat it to the operating
temperature.
b. Leak-check the impactor.
c. Sample with the impactor.
d. Disassemble the impactor; examine the stage catches and
impactor walls. Note any anomalies.
3. Substrates and re-entrainment checks
a. Check during pretest survey.
b. Check substrates (run blanks) to see if flue gas composition
changes significantly.
c. Examine deposits with a magnifier or microscope.
Procedures for Cascade Impactor calibration and operation in process
streams (revised 1979).
C-19
-------
APPENDIX C-3
RADIOCHEMICAL DETERMINATIONS OF
LEAD-210 AND POLONIUM-210
IN DRY INORGANIC AND BIOLOGICAL SAMPLES
BY ORP/EERF
-------
APPENDIX C-3
RADIOCHEMICAL DETERMINATIONS OF
LEAD-210 AND POLONIUM-210
IN DRY INORGANIC AND BIOLOGICAL SAMPLES
BY ORP/EERF
Principal
Polonium-209 and bismuth-207 tracers and lanthanum carrier are
added to a weighed aliquot of sample which has been dried at 100°C for
24 hours. The sample is solubilized by wet ashing. The radioelements
are coprecipitated as hydroxide with NH4OH. The hydroxide is redissolved
in acid and the bismuth and polonium are spontaneously deposited on a
clean copper disc.
210
The disc is beta counted for Bi, gamma assayed by Ge(Li) for
207 209 210
Bi and radioassayed by alpha spectroscopy for Po and Po. The
210
Pb can be determined by measuring ingrowth of its decay daughter
210
Bi which has a half life of five days.
Special Apparatus
1. Copper discs made from 0.6 mm thick copper sheet. Discs are
2.2 cm diameter with a 0.3 cm hole set 0.15 cm in from the
edges. The discs are coated on one side with an acid-resistant
paint.
2. -Constant temperature bath maintained at 80°C. Glycerol is
used as heat transfer fluid.
®
3. Teflon beakers. See Note 1.
4. Centrifuge.
5. Magnetic stirrer and stirring bars.
6. Glassware.
7. Alpha spectrometric system consisting of multichannel analyzer,
biasing electronics, printer, silicon surface barrier detector,
vacuum pump and chamber.
C-21
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Reagents
1. Ascorbic acid, crystalline reagent.
2. Ammonium hydroxide, 15M, 59 percent NH4OH reagent.
3. Hydrochloric acid, 12M, 37 percent HC1 reagent.
4. Hydrochloric acid, 6M. Dilute 500 ml of the 37 percent reagent
grade HC1 to one liter with distilled water.
5. Hydrofluoric acid, 29M, 48 percent HF reagent.
6. Lanthanum carrier, 10 mg La+ /ml. Dissolve 7.8 grams high
purity La(N03)3 6H20 in 250 ml distilled water.
7. Nitric acid, 16M, 70 percent HN03 reagent.
8. Bismuth-207 tracer solution. Approximately 10 pCi/ml.
9. Polonium-209 tracer solution. Approximately 1 pCi/ml.
Procedure
1. Add measured aliquot of Bi-207 and Po-209 tracers and 1 ml
lanthanum carrier to weighed one gram aliquot of sample in a
tf*l
Teflon beaker.
2. Add 15 ml 29M HF and 10 ml 16M HN03 and evaporate to near
dryness. Repeat this step.
3. Add three successive 10 ml volumes of 6M HC1. Evaporate to
near dryness following each addition.
4. Take up sample in 40 ml 6M HC1 and cover with watch glass
while warming sample for 30 minutes.
5. Transfer dissolved sample to 250-ml centrifuge bottle.
6. Make sample basic with careful addition of 15M NH4OH with
stirring.
7. Allow sample to stand for 30 minutes and centrifuge after
precipitate has formed.
8. Pour off supernate. Wash precipitate with 25 ml water.
Centrifuge and pour off wash water.
9. Dissolve precipitate by adding 1-ml increments of 12M HC1.
Use stirring rod to break up precipitate, using minimum amount
of HC1.
10. Place small magnetic stirring bar in centrifuge bottle and
slowly add 100 ml water with stirring.
C-22
-------
11. Transfer centrifuge bottle to constant temperature bath
maintained at 80°C.
12. If yellow color is evident, add ascorbic acid in 50-mg increments
until Fe color is gone.
13. Prepare copper disc by cleaning bare side with copper cleaner
and dipping disc in 12M HC1.
14. Suspend disc, using glass rod, into centrifuge bottle, keeping
disc under surface of liquid.
15. Maintain sample at bath temperature of 80°C for four hours.
16. Remove disc, rinse with water and air dry.
17. Mount on 32-mm planchet with double stick tape for radioassay.
C-23
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PREPARATION OF BISMUTH-207 STANDARD SOLUTION
Bismuth-207 decays by electron capture to lead-207m which emits a
gamma ray at 570 keV.
?fl7
1. Evaporate a measured aliquot of the Bi standard solution on
a copper disc.
2. Radioassay the disc with a Ge(Li) detector for 1,000 minutes
and record the net counts appearing under the 570 keV peak.
3. Radioassay the disc for beta activity using a beta counter
having a window of 7 mg/cm2 thickness. This assay determines
the contribution to the beta background from the bismuth-207
added to the sample.
Calculations
?10 210 Cl " [CR + (CRi . R>3
210Pb, 210Bi, pCi/unit sample = -± 2 a2_l_
2.22 R E Ve~Al
G! = Sample beta counts per minute.
CD = Beta background, counts per minute.
o
Cg. = Beta counts of bismuth-207 aliquot added to sample.
R = Chemical yield based on Ge(Li) counts of sample vs Ge(Li)
counts of aliquot added to sample.
E = Counter efficiency (7 mg/cm2 window).
A. = Decay constant for bismuth-210, minutes .
t = Time from separation to counting in minutes, using midpoints
of intervals.
V = Sample unit, liters or grams.
210Po, pCi/unit sample = (B-BJ E V T%.22
A = Gross sample counts which appear in the polonium-210
alpha energy region.
C-24
-------
A! = Background counts in the same alpha energy region as A
above.
B = Gross tracer counts which appear in the alpha energy
region of the tracer isotope.
B! = Background counts in the same alpha energy region as B
above.
E = Alpha detector efficiency.
F = Total calibrated tracer counts for same counting time as
sample counts.
A. = Decay constant for polonium-210, days .
t = Time from separation to counting in days.
V = Sample unit, liters or grams.
T = Counting time, minutes.
2.22 = dpm per pCi.
Lower Limit Detection (LLD)
4.66 CB T
LLD, Bi or Po pCi/unit sample = c D y 2 22 T
Cn = Background count rate.
T = Counting time; same for sample and background.
E = Alpha detector efficiency.
R = Fractional yield based on B-Bi/F in calculation, for Po.
210
See R, Bi calculation for Bi.
V = Sample unit, liters or grams.
2.22 = dpm per pCi.
This LLD calculation is valid if the sample counting time is equal to
the background counting time.
Notes
©
1. Teflon is a registered trademark of the duPont Company,
Wilmington, Delaware.
C-25
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References
1. Blanchard, R. L. "Rapid Determination of Lead-210 and
Polonium-210 in Environmental Samples by Deposition on Nickel."
Analytical Chemistry, 38, 189. 1966.
C-26
-------
APPENDIX D
FIELD ANALYTICAL RESULTS
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APPENDIX D-l
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APPENDIX D-2
FIELD GRAVIMETRIC LOGBOOK
(Journal Pages: 54-57, 70-101)
Note: 1. Unused pages marked out.
2. Logbook pages 58-69
intentionally omitted
per confidentiality agreement
(different test site)
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