AL/EQ-TR-1993-0002
EPA/600/R-94/214b
DEMONSTRATION OF SPLIT-FLOW VENTILATION AND RECIRCULATION AS
FLOW-REDUCTION METHODS IN AN AIR FORCE PAINT SPRAY BOOTH
ARMSTRONG LABORATORY
ENVIRONICS DIRECTORATE
mm S. Hughes, J. Ayer, R. Sutay
T
P AL/EQS-OL
O1 39 Barnes Drive, Suite 2
Tyndall AFB FL 32403-5323
N
G Acurex Environmental Corporation
555 Clyde Avenue
P.O. Box 7044
Mountain View, CA 94039
US EPA/AEERL
A MD-61
o Research Triangle Park NC 27711
0
p July 1994
A
-•• Final Technical Report for Period February 1991 - October 1992
O _
R .;.•;;.:;* :•::':;• •,:.•/•,: •.„-," ?•:.••
-------
NOTICES
This report was prepared as an a account of work sponsored by an agency of the United
States Government. Neither the United States Government nor any agency thereof, nor any
employees, nor any of their contractors, subcontractors, or their employees, make any warranty,
express or implied, or assume any legal liability or responsibility for the accuracy, completeness,
or usefulness of any privately owned rights. Reference herein to any specific commercial product,
process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily
constitute or imply its endorsement, recommendation, or favoring by the United States Government
or any agency, contractor, or subcontractor thereof. The views and opinions of the authors
expressed herein do not necessarily state or reflect those of the United States Government or any
agency, contractor, or subcontractor thereof.
When Government drawings, specifications, or other data are used for any purpose other
than in connection with a definitely Government-related procurement, the United States
Government incurs no responsibility or any obligation whatsoever. The fact that the Government
may have formulated or in any way supplied the said drawings, specifications, or other data is not
to be regarded by implication, or otherwise in any manner construed, as licensing the holder or any
other person or corporation, or as conveying any rights or permission to manufacture, use, or sell
any patented invention that may in any way be related thereto.
This technical report has been reviewed by the Public Affairs Office (PA) and is releasable
to the National Technical Information Service (NTIS), where it will be available to the general
public, including foreign nationals.
This report has been reviewed and is approved for publication.
D. WANDER, PliS MICHAEL G. KATONA, PhD
Manager, Air Pollution Control Technology Chief Scientist, Environics Directorate
EDWARD N. COPPOLA, Maj., USAF NEIL J. LAMB, Col, USAF, BSC
Chief, Environmental Compliance Division Director, Environics Directorate
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REPORT DOCUMENTATION PAGE
Form Approved
OMB No. 0704-0188
Public reporting burden for thii collodion of information it Mtimctad to average 1 hour per response, including the time for reviewing instructions, searching existing data sources, gathering
and maintaining the data needed, and completing and reviewing the collection of information. Send comments regarding this burden estimate or any other aspect of this collection of
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1. AGENCY USE ONLY (iff vt blank) I 2. REPORT DATE 3. REPORT TYPE AND DATES COVERED
1 940727 Final, 910215 to 921009
4. TITLE AND SUBTITLE
Demonstration of Split-flow Ventilation and Recirculation as
Flow-reduction Methods in an Air Force Paint Spray Booth
6. AUTHOR(S)
S. Hughes and J. Ayer; R. Sutay, CIH (Section VI)
7. PERFORMING ORGANIZATION NAME(S) AND ADDRESSES)
Acurex Environmental Corporation
555 Clyde Avenue
P.O. Box 7044
Mountain View, CA 94039
8. SPONSORING/MONITORING AGENCY NAME(S) AND ADDRESS(ES)
U.S. EPA Armstrong Laboratory
AEERL Environics Directorate
MD-61 AL/EQS-OL
Research Triangle Park, NC 2771 1 139 Barnes Drive, Suite 2
Tyndall AFB, FL 32403-5323
11. SUPPLEMENTARY NOTES
1. Responsible individual: Joseph D. Wander, (904) 283-6240
2. Office symbol: AL/EQS-OL
3. Availability of report is specified on inside front cover.
12a. DISTRIBUTION/AVAILABILITY STATEMENT
Approved for public release; distribution is unlimited.
S. FUNDING NUMBERS
Contract 68-D2-0063
Work Assignment 0/002
Program element 63723F
Project 21 03
Task 70
Work unit accession 97
8. PERFORMING ORGANIZATION
REPORT NUMBER
FR-93-115
10. SPONSORING/MONITORING
AGENCY REPORT NUMBER
AUEQ-TR- 1993-000 2
EPA/600/R-94/214b
12b. DISTRIBUTION CODE
13. ABSTRACT (Maximum 200 wonti)
During a series of painting operations in a horizontal-flow paint spray booth at Travis AFB, CA,
baseline concentrations of four classes of toxic airborne pollutants were measured at 24 locations
across a plane immediately forward of the exhaust filters, in the exhaust duct, and inside and outside
the respirator in the painter's breathing zone (BZ). The resulting data were analyzed and used to
design a modified ventilation system that (1) separates a portion of the exhaust exiting the lower
portion of the booth, which contains a concentration of toxic pollutants greater than the average at
the exhaust plane (split-flow); and (2) provides an option to return the flow from the upper portion of
the exhaust to the intake plenum for mixing with fresh air and recirculation through the booth
(recirculation). After critical review by cognizant Air Force offices, and an experimental
demonstration showing that a flame ionization detector monitoring the air entering the booth is able
to detect excursions above the equivalent exposure limit for the solvents in the paint, the exhaust
duct was reconfigured for split-flow and recirculating ventilation. A volunteer painter was briefed on
the increased risk of exposure during recirculation, and on the purposes and possible benefits of this
study. He then signed an informed consent form before participating in the recirculation tests. A
series of tests generally equivalent to the baseline series was conducted during split-flow and
14. SUBJECT TERMS
Air pollution, emission control technology, exhaust
recirculation, paint spray booth, ventilation
15. NUMBER OF PAGES
Vol. 1,132; Vol. II, 179
16. PRICE CODE
17. SECURITY CLASSIFICATION 18. SECURITY CLASSIFICATION OF 19. SECURITY CLASSIFICATION 20. LIMITATION OF ABSTRACT
OF REPORT THIS PAGE OF ABSTRACT
Unclassified Unclassified Unclassified
NSN 7540-01-280-5500
Standard Form 298 (Rev. 2-89)
Prescribed by ANSI Sid. 239-18
298-102
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Unclassified
SECURITY CLASSIFICATION OF THIS PAGE
recirculating ventilation, and three tests were performed during only split-flow ventilation. Data from the
two sets of tests show that pollutants concentrate toward the bottom of the booth during ordinary
painting operations; that local processes associated with circulation near the paint spray gun contribute
far more to the net exposure to the painter than do toxic pollutants in the recirculated air stream; and
that, under well-ventilated conditions, including split-flow and recirculation of a large fraction of the
exhaust air, equivalent exposures to airborne toxic pollutants (calculated as the sum of 8-hour, time-
weighted concentrations of toxicants divided by their respective Permissible Exposure Limits) should not
exceed 0.25 in the intake air. An economic analysis of costs to implement thermal or catalytic
incineration, with and without flow reduction by split-flow and recirculating technologies, projects
substantial savings, such that the payback periods for inclusion of flow-reduction technology during
installation of the control device are about 1 year. The recirculation of air in the paint spray booth did not
result in an increase in air contaminants that would exceed the capability of proper respiratory
protection. The magnitude of the incremental increase in exposure derives primarily from particulates in
the recirculated air. This is defined by the particulate removal efficiency of the paniculate controls, which
can be compromised by improper maintenance. However, with proper design, installation, and
maintenance, the increment to risk is normally less than the round-off errors in the calculation of net job-
related risk. Because the cost benefit is obtained at an increase of risk of exposure to painters, the
acceptability of this cost-benefit tradeoff will have to be resolved by industrial hygiene functions at both
policy and local levels before this advance can be implemented at Air Force installations.
Unclassified
SECURITY CLASSIFICATION OF THIS PAGE
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SUMMARY
OBJECTIVE
The objective of this program was to demonstrate that split-flow and recirculating
ventilation, individually and in combination, are safe and cost-effective methods of reducing paint
spray booth exhaust flow rates to lower the costs both of conditioning intake air and of
controlling volatile organic compound (VOC) emissions in exhaust air.
B. BACKGROUND
This study was part of an extended program of investigations into the cost and efficacy
of innovative approaches for bringing U.S. Air Force industrial operations into compliance with
current and anticipated air pollution environmental standards. Adequate ventilation of paint spray
booths requires the movement of large quantities of air, which are slightly contaminated during
passage through the booth. Air exhausted from this process requires decontamination, which,
although technically achievable at operating flow rates, can be prohibitively expensive. Because
emission-control costs depend on the volume of exhaust air being treated, considerable savings
can be realized through the application of an acceptable flow-reduction method.
A first principle of industrial hygiene is to employ engineering controls to their limit before
invoking personal protection. In dealing with exposures to airborne toxics, the mainstay
engineering device is enhancement of ventilation. However, increased ventilation creates
enormous volumes of slightly contaminated air, which must be treated before discharge and, in
many situations, the cost of such treatment is excessive. In such circumstances, a judgment
must be made about the relative cost in increased exposure compared to the economic benefit
in decreased operating cost. The goal of this study was to provide experimental data to support
the development of a general Air Force position and objective criteria for local decisions about
the acceptability of using flow-reduction methods in paint spray booths, based on local health-
risk/cost-benefit considerations.
C. SCOPE
This study comprised two sets of experimental measurements in Booth 2, Building 845,
Travis Air Force Base (AFB), California, plus the results of an ancillary effort conducted at
Research Triangle Institute (RTI) to verify experimentally that the flame ionization detector (FID)
used in the ventilation control loop is within its linear response range at the equivalent exposure
limit for the mixture of solvents present in the mixed topcoat. The first set of experimental
measurements was a baseline characterization of the distribution of toxic pollutants at the
exhaust face and in the exhaust duct of Booth 2. These data, the RTI results, and the test plan
for the second set of tests were reviewed by HQ AFLC/SGBE before approval was given to
proceed with the recirculation tests. The test plan and engineering drawings were reviewed by
the Fire Department, Safety Office, and Civil Engineering Office at Travis AFB and approved
before implementation. For the second set of tests, the ductwork in Booth 2 was reconfigured
to separate exhaust streams from the top and bottom of the booth (split-flow) and to return the
upper exhaust stream to the intake plenum for recirculation through the booth. The volunteer
painter was briefed and signed an informed consent form before participating in the study.
During separate painting sessions, several sets of concentration measurements were made of
VOCs, particulates, heavy metals, and isocyanates. Equivalent exposures (£„) were calculated
from these data, and projections of Em were made for a range of recirculation ratios, together
iii
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with an economic analysis of the corresponding costs to install flow reduction technology and
apply VOC emission control devices.
D. METHODOLOGY
Per standard Travis AFB policy, painters in Booth 2 wear a protective jump suit, a
separate hood, and an airline respirator. To determine exposure concentrations, sampling was
performed simultaneously inside and outside the respirator, at 24 locations at the exhaust face,
in the exhaust ducts, and, during the second set of tests, at three locations at the face of each
of the two intake filters. To determine environmental contributions to the load of pollutants,
background air samples were collected at the back of the booth prior to the release of any paint-
derived materials. Standard sampling methods used were National Institute of Occupational
Safety and Health (NIOSH) Method 1300 (integrated measurement of individual organic species),
Bay Area Air Quality Management District (BAAQMD) Method ST-7 and U.S. Environmental
Protection Agency (EPA) Method 25A (continuous measurement of total organic concentration),
Occupational Safety and Health Administration (OSHA) Method 42 (filter faces and ducts) and
NIOSH Method 5521 (painter and ducts) (isocyanates), EPA Method 5 and NIOSH Method 500
(particulate), and EPA Draft Multiple Metals and NIOSH Method 7300 (metals). Paint usage was
determined by weighing the gun after each filling and at the end of each painting session. The
percent volatile content of the paint was determined gravimetrically, as percent weight loss to
evaporation. Airflows were measured with an anemometer (American Conference of
Governmental Industrial Hygienists [ACGIH]) in the booth and with a pitot tube (EPA 2) in the
exhaust ducts. Painting start and stop times were recorded manually by an observer, stationed
at the rear of the booth, who also noted the dimensions and locations of workpieces painted,
coatings applied, and other details. Projections of equivalent exposures at different recirculation
ratios were calculated by a Lotus 1-2-3 program written at U.S. EPA-Air and Energy Engineering
Research Laboratory (AEERL).
E. TEST DESCRIPTION
In both test series, representative workpieces were prepared and coated according to
normal operating procedures. During each such painting run, measurements were made of one
of the four pollutant classes using the methods specified in Section D. A typical painting session
lasted 30 to 90 minutes, and included postpainting cleaning of the paint spray gun with methyl
ethyl ketone (MEK) and tidying up of the area. In general, two sets of tests were accomplished
during an 8-hour shift, corresponding to a typical workday. A complete series of blood chemistry
parameters was determined for the painter at the conclusion of the testing.
F. RESULTS
Concentrations of airborne toxic pollutants are recorded in the tables of the report.
Strontium chromate occurs as the major contaminant during primer coating and was the largest
contributing factor to the £m. Organic exposures were minor during all painting exercises,
except that high isocyanate exposure occurred outside, but not inside, the painter's respirator
during topcoat application inside a comfort pallet (caused by airflow restrictions in the closed
space, and unrelated to the mode of ventilation in the booth). The newly constructed
recirculation duct was a source of several metals. These metals were included in Em
calculations, but the concentrations are expected to decrease after the newly constructed
surfaces are blown clean. Contributions to Em from recirculation are significantly less than the
Air Force criterion of 0.25 imposed by HQ AFLC/SGBE for these tests, and much less, in
iv
-------
general, than the contribution from the painting process. The painter showed no evidence of
overexposure during the posttest medical evaluation.
G. CONCLUSIONS
Data support the prediction that workplace exposure levels during recirculation of paint
spray booth exhausts, especially combined with split-flow extraction of the pollutant-enriched
lower portion of the exhaust stream, can be maintained less than an arbitrarily selected criterion
(here, Em = 0.25). Flow splitting as a technology is only marginally effective; however, in
combination with recirculation, it acts to lower the concentrations in the recirculated stream at
a given rate of recirculation. Computational projection of Em to larger recirculation rates, and
interpolation of results of an earlier economic analysis of scale-related costs to decontaminate
exhaust air, indicate that available cost savings allow projected payback periods on the order of
1 year for thermal or catalytic incineration.
H. RECOMMENDATIONS
Improvements should be examined to augment or replace present-generation filter and
water particulate control systems. Concurrently, or when the improved technologies satisfy local
standards, a combination of flow reduction and VOC control should be implemented in an area
of intense regulatory pressure as the definitive prototype. A standardized set of criteria should
be established to guide site selection, design, installation, and maintenance.
v
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PREFACE
This final report was prepared by Acurex Environmental Corporation, 555 Clyde Avenue,
Mountain View, CA 94043, under Contract No. 68-D2-0063, for the U.S. Environmental Protection
Agency (EPA), Air and Energy Engineering Research Laboratory (AEERL), and the Armstrong
Laboratory Environics Directorate (AL/EQ), 139 Barnes Drive, Tyndall Air Force Base (AFB) FL
32403-5323. The industrial hygiene evaluation was performed by Clayton Environmental
Consultants, 1252 Quarry Lake, Pleasanton, CA 94566.
This report describes measurements of background concentrations of airborne toxic
pollutants in Booth 2, Building 845, Travis AFB, CA; design and construction of modifications to
the booth ventilation system; measurements of airborne toxic pollutants in the modified booth
during split-flow and concurrent split-flow and recirculating ventilation; and a projective analysis
of equivalent personnel exposures and net costs to operate flow reduction and emission control
systems at varying recirculation ratios. The work was performed between February 1991 and
September 1992. The Air Force project officer was Dr. Joseph D. Wander. EPA project
managers were Charles H. Darvin and Jamie K. Whitfield.
Indispensable cooperation and support were provided by a number of Air Force functions.
Ted Liston (60 EMS/MAEFP) provided facilities in Building 845 and practical advice; Terry
Kirkbride (60 EMS/MAEFP) and Mark Sandy (60 ABG/EM) managed coordination with cognizant
Travis functions and solicited volunteer painters; Sgt. Bill Fleming and Bill Harrison painted during
the baseline and split-flow tests, respectively; Richard Smith painted during the recirculating
ventilation tests; TSgt. Haugen (DGMC/SGPM) saw to the posttest evaluation of Mr. Smith and
secured his release of the test results; Det 6 AL/SAO, Brooks AFB TX, performed metals and
isocyanate analyses; Major John Seibert, Det 6 AL/EHI and the designee of Col. Bruce Poitrast,
AL/OE-CA, was an active contributor to discussions of baseline data and the test plan for the
recirculation tests; Col. Phil Brown, HO AFLC/SGBE, accepted responsibility for authorizing the
performance of the recirculation tests, after several iterative discussions of these baseline results
plus data and conclusions from experimental verification of the capability of flame ionization
detector (FID) technology to reliably detect equivalent exposure limit of a complex (specified)
mixture of paint solvents. Major Steve Bakalyar, AL/OEMI, offered constructive suggestions and
contributed to the final version of this document.
vii
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TABLE OF CONTENTS
Section Title Page
APPENDIX D-BOOTH MODIFICATION DESIGN AND
CONSTRUCTION PACKAGE 1
APPENDIX E - ORGANIC DESORPTION STUDY 25
APPENDIX F - REDUCED DATA FOR THE BASELINE TEST
SERIES 30
APPENDIX G -REDUCED DATA FOR THE POSTMODIFICATION
TEST SERIES 47
APPENDIX H- QUALITY ASSURANCE/QUALITY CONTROL
EVALUATION 158
APPENDIX I — ECONOMIC CALCULATIONS 163
APPENDIX J - EXAMPLE CALCULATION WORKSHEET FOR
PERCENT RECIRCULATION VERSUS PERCENT
PARTICULATE REMOVAL EFFICIENCY 168
IX
(The reverse of this page is blank)
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APPENDIX D
BOOTH MODIFICATION DESIGN AND CONSTRUCTION PACKAGE
The booth modifications are illustrated in the accompanying schematics and described
briefly below.
A. DUCT MODIFICATIONS
Downstream of the existing exhaust blower (exhaust fan 1) a 48-inch-diameter sheetmetal
tee was installed in the existing duct. Two motor-operated, 48-inch-diameter air dampers were
installed on the exhaust ports of the tee (dampers 1 and 2). Damper 2 was installed on the
downstream side of the tee and between the tee and the continuation of the existing 48-inch-
diameter duct. It controls the flow of exhausted gases to the atmosphere outside the building.
Damper 1 was installed on the branch side of the tee and controls the flow of exhausted gases
to the inlet duct for recirculation. A new 48-inch-diameter sheetmetal duct was installed between
damper 1 and the existing fresh air supply duct.
Control of the two damper air motors is regulated by Analysis Safety Valve (ASV)-1
(ASCO Model 834911), a four-way dual solenoid valve, which allows plant air to flow to or vent
from the air motors according to the feedback control system (discussed below). In the event
of power loss, the solenoid valve fails to the fail-safe mode, i.e.-, the single-pass position, which
closes damper 1 and opens damper 2, thus diverting all exhaust gases to the atmosphere
outside the building.
In addition to modifications to the existing ducts, a new 30-inch-diameter axial blower and
duct was installed to vent the lower chamber of the plenum.
B. FEEDBACK CONTROL SYSTEM
A failsafe damper interlock control system was designed to respond to an instantaneous
emission peak exceeding the STEL action level and to a 60-second emission level at or above
the TLV.
The interlock system (see drawings 8380E100 and 8380E101) was equipped with the
following features:
• Total unburned hydrocarbon (TUHC) analyzer (Ratfisch Instruments type RS 55CA
heated total hydrocarbon analyzer FID) (ASE-1/AST-1).
• Failsafe controls (ASA-1 /ASV-1):
— An instantaneous interlock to begin single-pass operation when STEL
concentration action level is exceeded.
— An adjustable timer (set at 5 minutes) to ensure single-pass operation for a
predetermined time after STEL or TLV interlock activation, prior to converting
back into the recirculation configuration.
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— An adjustable timer (set at 60 seconds) to delay operation of the TLV
concentration interlock for 1 minute while continuing monitoring operations. If,
after 1 minute, the concentration is still above TLV, the system initiates the single-
pass mode.
— An indicator light to indicate that the 60-second TLV concentration timer is "on."
— An interlock to convert the system to single-pass mode if the hydrocarbon
analyzer power is turned off or its flame goes out.
— A solenoid valve wired and plumbed to return to the single-pass operation mode
whenever there is a power loss.
C. PERMIT VARIANCES
At the start of this study, the paint booth was operational and permitted for use in the
single-pass mode. In conversations with the Bay Area Air Quality Management District
(BAAQMD), it was determined that a new permit to operate the booth after modification was
unnecessary; a notification letter to BAAQMD in advance of the modification sufficed.
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SUPPLY AIR
I BLOWER #1
SUPPLY AIR
BLOWER #2
EXHAUST
FAN #1
' SUPPLY AIR
FILTER
EXHAUST AIR
FILTERS
PAINT BOOTH
SUPPLY AIR
FILTER
Process and Instrumentation Diagram
Travis AFB Building 845
Paintbooth No. 2 Prior to Modification
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NOTES:
1. ALL DIMENSIONS
ARE APPROXIMATE
AND SHALL BE FIELD
VERIFIED.
2. TRANSITION PIECE
SHALL BE MADE IN
SECTIONS WHICH CAN
BE PASSED THROUGH
THE EXISTING
PERSONNEL DOOR.
3. TRANSITION PIECE
SHALL INCLUDE ALL
SUPPORTS AND
FASTENERS.
30" 0 GALVANIZED
STEEL SPIRAL LOCK-
SEAM DUCT. TYP.
(UNITED McGILLUNI-
SEAL ROUND DUCT
AND FITTINGS, 2-10
INCHES W. G., OR
APPROVED EQUAL)
22 GAUGE MINIMUM
30" 0 EXHAUST FAN
TRANSITION PIECE
FABRICATE FROM
MINIMUM 22 GAUGE
GALVANIZED SHEET
METAL (SEE NOTE
2 AND DRAWING
8380M107)
Lower Exhaust Plenum Chamber
Transition Piece and Exhaust Duct Isometric
for Travis AFB Building 845 Paintbooth No. 2
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01
EXHAUST
FAN 42
CHEMICAL
FIRE
SUPPRESSANT
Process and Instrumentation Diagram
Travis AFB Building 845
Paintbooth No. 2 After to Modification
-------
~
1
*> ALL VAPOM TO THE ATUOSPHERE
(THE SWITCH KBOE THE COHTML BOX (SEE DHAWMO OMEtOO) • SET M THE AB PC6ITOM)
ASCO 834911
Position Diagrams of Damper Control 4-Way Solenoid Valve ASV-1
Describing Various Energized and De-energized Positions
and the Effect on Dampers No. 1 and No. 2
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PULL BOX
-------
NORTH
ADJACENT PA1KT
SPRAY BOOTH
I
I-
ADJACENT WUNT
snur loom
6KOLE (TOUT
STRUCTURE
AH. DUENSIONS SHOWN ARE APPROIIMTE AND SHAU. BE VERFIED N
THE FdD BY THE CCNTRACTOA.
EnEIDOII 1ULDMO WAU.
nATPORM
I OECX RATE)
TRAVIS A.F.a PAINIBOOTH
"" """"'"
BUILDING S4S
PLAN VIEW - EXISTING
8380M10l|,"T, I
(The reverse of this page is blank)
-------
i
I-
V T SOUARE M1AKE
DUCT NO
-------
4--ES>
r<- TOP OF riATKMM
CONCRETE BULDMO
FOOTNO -
MEGH FLTER BANK
I PLEATED «.TI
13
(The reverse of this page is blank)
-------
NORTH
NOTES:
I. PROVDE A DRV CHEMCAL FOE SUPPRESSION SYSTEM FOR IXC PLENUM
CREATED MSDC 1HE HEW TRANSITION PCCC. TMC SYSTEM SMALL CCNSBT
OF THREE (1) AUTOMATCALLV ACTUATED SPRAY HEADS CONNECTED
THROUGH A MANUALLY RESETABLE SWITCH TO A CANNBTOA OF CRT
CHEMCAL SUPPRESSANT. THE MANUALLY RESETTABLE SWITCH SHALL BE
CONNECTED TO THE EXMTMO ALARM «r»TEU WHICH PRESENTLY •
ACTIVATED f THERE * A FRf H THE PAMTBOOTH. THE F«E
SUPPRESSION SYSTEM iHAU BE ANBUL SPA M NDUSTRUL FRE CONTROL
SYSTEM (COMPLETE AND N8TAU£D TO COMfLV WITH HFPA M. ALL STATE
AND LOCAL LAWS AMD REGULATIONS. UL L0TMOS. AMD tfSURANCE
CCUFANY REOUAEMENT8) OR APPROVED EQUAL
1. MTERCONNECT THE NEW XT • GO4AUST FAN WMV4O WTTH THE
START/STOP CONTROLS FOR THE EX18TMO SUPPLY AMD GWAUST FANS SO
THAT ONE SWITCH LOCALLY ACTIVATES ALL THREE FANS.
1. PMOVDC A NEW NMNOMETER. OF THE SAME IMNUFACTURER. DE&K3N AND
RWOI AS THE EJOSTNO IIMCTKTIR. ADJACENT TO THE EXBTMO
MANCHCTER. AND CONNECT fTB PORTS BETWEEN THE PAMTBOOTH
OKRATMO AREA AND THE NEW PLENUM CREATED JKPC THE NEW
TRANSmON PKCI. TO KOCATE WHEN THE FITER MCDK HEEDS CHAHOtn
t CUT KTO THE *V • DUCT WHERI SHOWN AND PROVCC A NEW TEE.
• PWVDf A NEW W • BUM EXHUJST FAN WHERE SHOWN. FAN SHALL
BE RATED FOR Zt.000.fci AT Ur W.C. DRNI MOTOR BHALLM WOVAC.
> PIKtl, W HERTl TEFC. AND OP ADEQUATE HORSEPOWER AND CORRECT
nm FOR BOTH THE PAN AND ITS VARHU PITCH SHEAVt FAN SHAFT
SPIED CONTROLLER. THE VARMHB FfTCH SHEAVI SET SMALL PROVDC AN
RPM TUMNDOWN RATD OF >: I. AND SHALL BC WOOD* Na PRO - MO - W OR
DUCTMO • MMETRB. FOR
OETAUL PROVBf NEATLY
FMEHED PENETRATIONS
THROUOH THE PAMTBOOTH WALL.
THEBUmsn WALL. AHO TMI
. OUTDOOR PLATFORM PAMT-
BOOTH PENETRATION SHALL BE
SEALED ABnOHT BUUMO
WALL PENETRATION SHALL BE
WEATKERTIOHT. MSTALLATKM
SHALL NCLUOE ALL SUPPORTS
AND FASTENERS.
niOVDf *V • OALVAMnD
STEEL STOW. LOCKSEAM OUCT
(IMTED MaOSX UMSCAL ROWD
DUCT AND RTTMOS, X • 10 MCKES
WO, OR APPROVED EOUAL) *>
PROVM tT » DAMPER (SEE
NOTE 41
F*E SUPPRESSHN SYSTEM DRY
CHEMCAL SUPPRESSANT CANNBTOR
PROVDC 4'
-------
ExtSTNO DUCTWORK
PROVIDE 4- ff e DAMPER (SEE
NOTE 3)
PROVDE 4'.
-------
PnOVOE XT • GALVANIZED
STEEL SPIRAL LOCKSEAM DUCT
(SEC DRAWMO V3MH107. 6ft.(1
FlOW TRANSmoN PCCC AND
DUCTNO • BOMETRC. FOR
DETAL8). PROVDE NEATLY
FMBHED PENETRATIONS
THROUGH THE PAMTBOOTH WALL.
THE BULDNd WAU., AND THE
OUTDOOR PLATFORM. PAINT-
BOOTH PENETRATION GHAU BE
SEALED AJTTO4T. BULDNO
WALL PENETRATION BHAU BE
WEATHEATUHT. M8TALUTKM
SHALL HCLUDE All SUPPORTS
AND FASTENERS-
- TOP Of DUCT IS
47 0- ABOVE IHE
CONCRETE FLOOR Of
THE BUUWG
EXISTMO DUCTWORK
PROVIDE 4'
PROVDE EXHAUST
FAN < SEE NOTES 1
AND 6)
PROVIDE A DRV CHEMKAL FRE SUPPRESSION SYSTEM FOR THE PLENUM
CREATED WSOE THE NEW TRAMSTTKM PCCE. THE SYSTEM SHALL CON&6T
OF THREE ()) AUTOMATICALLY ACTUATED SPRAY HEADS CONNECTED
THROUOH A MANUALLY RESETABLE SWnCH TO A CANNBTOfl OF DRY
CHEMCAL SUmCSSANT. THE MANUALLY RESETTABLE SWTTCH SHALL BE
CONNECTED TO THE £*«TNO ALARM SYSTEM WHCH PRESENTLY B
ACTIVATED f THERE B A FHE M THE P AWT BOOTH THE FtftE
SUPPRESSION SYBTEM SMALL M ANSUL SPA U> MDUBTRIAL FIRE CONTROL
SYSTEM (COMPLETE AND HSTALLED TO COMPLY WTTH NFPA W. AU. STATE
AND LOCAL LAWS AND REOULATDNS, UL LBTNOB. AND NSURANCE
CCMPANY REOUttEMENTR ) OR APPROVED EQUAL.
MTERCGNNECT THE NEW XT • EXHAUST FAN WMMO WTTH THE
START IflOf CONTROLS FOR THE EXtSTNO SUPPLY AND EXHAUST FANS SO
THAT ONE SWITCH LOCALLY ACT MATES ALL THREE FANS.
PROVDC A NEW MANOMETER, Of THE SAME MANUFACTURER. DESIGN. AND
RANOE AS THE CXtSTMO MANOMETER. ADJACENT TO THE EXIST WO
MANOMETER ON THE WEST WALL BY THE PERSONNEL DOORS. AND
CONNECT fT» PORTS BETWEEN THE PAINTBOOTH OPERATMO AREA AND THE
NEW PLENUM CREATED fffSDE THE NEW TRANSITION PCCE TO MDCATE
WMENTHE FLTEfl MEDH NEEDS CHANOMa
. CUT NTO THE «"«* 0 DUCT WHERE SHOWN AND PROVDC A NEW TEE
NEW Vff 0 TEf AND DUCTNO SHALL BE OALVANIZED STEEL SPIRAL LOCK
SEAHZOOAiNX MMMUM ( UNTTED McOU. UMSEAL. 2 10 NCHE6 W.O. OR
APPAOVCO EOUAL).
. PROVOC A NEW XT 0 N4.ME EXHAUST FAN WHERE SHOWN. FAN SHALL
BE MATED FOR Z&OOOcbn AT SJT W.C. DRTVE MOTOR SHALL BE MOVAC.
3 PI MI. SO HERTZ. TEFC, AND OF ADEQUATE HORSEPOWER AND CORRECT
MM KM BOTH THE FAN AND (T» VARIABLE PfTCH SHEAVE FAN SHAFT
SPEED CONTMUER. THE VARIABLE PITCH SHEAVE SET SHALL PROVDE AN
RPU TURNDOWN RATIO Of 3: I. AND SHALLK WOOCTS N^ PRO 300- W OR
APPROVED COUAI-
PROVDC NEW 4*
-------
FU- I
2A
ANAIYZER
FLAMEOUT
i o
I
I
ANALYZER
CONCENTRATION
INTERPOSING
RELAY
CLOSES FOR
ANALYZER
POWER ON
OPENS FOR
FLAME OUT
OPENS ON HIGH
CONCENTRATION
OPENS AFTER HIGH
CONCENTRATION
FOR 60 SECONDS
ANALYZER SWITCH I—rTT—I TTT"
TERMINAL BOARD I I _ I I 1,1
LOCATED NEAR
THE ANALYZER
1 USE STANDARD 3 PRONG 120V LNG PLUG
FOP POWER CONNECTION
2 CR I ALLEN BRADLEY 700-N400A1
3 TR--1- CAUROIAN PET 14«1 WITH II-PIN
OCTAL SOCKET
SWITCH No 12345679
X.ON XXXOOXOX
< TR - 2 POTTER AND BRUMFIELD
CWB - 3» - 76000 WITH 11 - PIN OCTAL SOCKET
SWITCH SETTINGS: OP. SEC. 10-100
F'lisiinunoN ron WOMEN-
IAIIY MANUAL OVLMFtlDE Or
THE INSTRUMENT CONCEN-
TRATION INTERLOCK ( FOR
SPRAY GUN CLEANING )
RELAY TO CONTROL
THE ACTUATORS
ANALYZER POWER
SWITCH INTERLOCK
S MINUTE MINIMUM ACTIVATION
OF THE ACTUATORS
60 SECOND HIGH
CONCENTRATION TIMER
60 SECOND HIGH CONCENTRATION
TIMER -ON" INDICATION
SOLENOIDS "A- > -D- ON VALVE ASV • I TO CONTROL THE PNEUMATIC
MOTORS ON DAMPERS 1 > 2
•A" » -B- ENERGIZED OPENS DAMPER I AND CLOSES DAMPER 2
•A- ENERGIZED » V DE-ENERGIZED LOCKS DAMPERS IS POSITION
•A- S -B- OE ENEFCIZED CLOSES DAMPER I AND OPENS DAMPER 2
LIMIT SWITCHES ZSl - 1 « ZSH 1 OPCN WHEN "A- « -fl- ARE IN THE
•ENERGIZED POSITION- AND DAMPER 1 IS FULLY OPEN AND DAMPER 2
IS FULLY CLOSED
AS BUILT
RELEASED FOR CONSTRUCTION
OJT
DJT
D J. TATE
6-24-91
B. DOSS
B. DOSS
6-24-91
ACUREX
t Corporation
Env4ionm>nl«l SyH»fm Division
TRAVIS A. F. B. PAINTBOOTH
ADDED FUSE « OUTLET. REVISED NOTES
DJT
B. DOSS
9-25-91
ADDED SOLENOID B i SWITCHES
DJT
7-26-91
PROJECT NO.
6380.060
CONTROL SCHEMATIC
RELEASED FOR BID
DJT
NONE
DESCRIPTION
APFO OAIE
REVISIONS
REFERENCE DRAWINGS
rf ••*•«»' ««-. {
j (V-«^ *C
B
REV
E
21
(The reverse of this page is blank)
-------
TUHC ANALYZER
RATFISCH RS55CA
(ASE- 1 & AST-1 )
RIS ET-1218
VOLTAGE ALARM ( ASA -1)
4 - 20 mA J2'5
OUTPUT J2.4
0- 10 V J2-3
OUTPUT J2.,
STRIPCHART
RECORDER
(ASR-1)
4 - 20 mA, 250 OHM
INPUT IMPEDANCE
115 VAC POWER
NORMALLY ENERGISED
( FAILSAFE ) CONTACTS
SEE CONTROL
SCHEMATIC
AS BUILT
OJT
6-23-92]
0. J. TATE
6-24-91
B. OOSS
B. DOSS
6-24-91
6-24-91
ACUREX
* Corporation
Em»iKxim>filal SYfl«ms Division
TRAVIS A. F. B. PAINTBOOTH
RELEASED FOR CONSTRUCTION
DJT
B. OOSS
9-25-91
ADDED INSTRUMENT NUMBERS
pnouecT NO
8380.060
ANALOG WIRING DIAGRAM
RELEASED FOR BID
OJT
NONE
REVISIONS
REFERENCE DRAWINGS
B
8380E101
SHEET I REV
1 OF 1
23
(The reverse of this page is blank)
-------
APPENDIX E
ORGANIC DESORPTION STUDY
25
-------
HATIONU EXPRESS LABORATORIES, INC.
Mid-Pacific Invironmentol Laboratory, Int.
625B Clyde Avenue
Mountain View, CA 94043
(415) 964-0844
FAX (415J 961-7113
June 4, 1991
Ms. Jackie Ayer
Acurex Engineers
555 Clyde Avenue
Mountain View, CA 94043
Ms. Ayer:
Here are the NIOSH 1300 information I promised you. Our final
report to you has all been corrected for desorption efficiency.
The desorption efficiency study was performed at three levels
approximately lOOug, 700ug, and 1400ug per tube. The MDL study
was performed using the same amount as level I of the desorption
efficiency study. The correction factor used in calculating your
NIOSH 1300 is slighly different from this set I am sending to
you. The only difference is that I had normalized all recovery
greater than 100 percent to 100%. This set I am sending you has
was not been normalized for recovery greater than 100 percent.
There is only about 0.1 to 0.6 percent difference between the
numbers. If you want your reports revise using the new
correction factor please let me know.
Sorry this took so long. I hope this did not cause you any
inconvenience with your project.
Sincerely,
Daniel Mew,
GC Section Manager
Mid-Pacific Environmental Laboratory Inc.
National Express Laboratory
.'ended paper
26
-------
MID-PACIFIC ENVIRONMENTAL LABORATORY
Instrument ID: 3400-2 (DB624 60m column)
Date: 4/25/91
Page 2
Desorption Efficiency Study - Level l
MEK
ETHYLACETATE
2-BUTANOL
N-BUTANOL
METHOXYACETONE
ETHOXYETHANOL
MIBK1
TOLUENE
BUTYLACETATE
ETHYLBENZENE
M & P XYLENE
PMGE ACETATE
O-XYLENE
2-EOE ACETATE
2-MOE ETHER
Extract
cone.
37.00
35.00
38.00
33.00
19.00
28.00
31.00
34.00
26.00
34.00
34.00
38.00
35.00
38.00
38.00
Al
104.82
103.64
101.60
93.65
49.37
21.35
104.61
103.57
105.15
105.76
98.47
105.00
101.18
106.95
66.66
A2
104.57 .
103.55
99.80
92.62
49.11
21.59
103.58
102.63
104.17
104.81
134.76
104.47
101.46
106.23
69.15
A3
104.99
103.29
101.38
93.33
48.08
23.88
103.50
102.51
104.05
104.31
119.45°
103.52
101.42
100.73
71.00
Desorption Efficiency Study - Level
MEK
ETHYLACETATE
2-BUTANOL
N-BUTANOL
METHOXYACETONE
ETHOXYETHANOL
MIBK1
TOLUENE
BUTYLACETATE
ETHYLBENZENE
M & P XYLENE
PMGE ACETATE
O-XYLENE
2-EOE ACETATE
2-MOE ETHER
Extract
cone.
185.00
175.00
190.00
165.00
95.00
140.00
155.00
170.00
130.00
170.00
170.00
190.00
175.00
190.00
190.00
Bl
101.28
100.77
97.92
96.04
82.71
65.70
99.92
99.48
101.05
100.37
108.54
99.14
96.08
98.93
76.16
B2
92.99
92.15
89.68
87.79
74.71
58.65
91.01
90.54
91.88
91.55
89.66
90.21
87.66
90.42
68.80
B3
99.24
98.52
95.49
94.12
80.82
63.85
97.57
97.04
98.33
97.85
95.80
96.58
93.62
96.43
73.87
A4
104.18
101.56
99.92
93.04
49.52
22.33
102.03
101.11
103.08
103.47
129.22
102.90
100.65
105.04
66.08
2
B4 %
100.94
99.73
97.36
95.48
82.38
65.98
98.80
98.25
99.45
99.15
97.12
97.81
94.92
97.79
75.16
Average
%Rec.
104.64
103.01
100.67
93.16
49.02
22.29
103.43
102.46
104.11
104.59
120.48
103.97
101.18
104.74
68.22
Average
Rec.
98.61
97.79
95.11
93.36
80.16
63.54
96.82
96.33
97.68
97.23
97.78
95.94
93.07
95.89
73.50
27
-------
Page 3
Desorption Efficiency Study - Level 3
Extract
cone.
MEK 370.
ETHYLACETATE 350.
2-BUTANOL 380.
N-BUTANOL 330.
METHOXYACETONE 190.
ETHOXYETHANOL 280.
MIBK1 310.
TOLUENE 340.
BUTYLACETATE 260.
ETHYLBENZENE 340.
M & P XYLENE 340.
PMGE ACETATE 380.
O-XYLENE 350.
2-EOE ACETATE 380.
2-MOE ETHER 380.
00
00
00
00
00
00
00
00
00
00
00
00
00
00
00
Cl
99.69
98.78
96.79
95.38
85.83
81.10
98.84
98.12
99.14
98.08
97.76
97.26
93.79
96.97
79.70
C2
100.85
99.88
97.87
96.61
87.10
78.81
99.33
98.74
99.86
98.78
97.40
97.89
94.46
97.90
79.86
C3
99.40
98.82
96.51
95.10
85.60
77.96
97.67
97.00
98.49
97.52
96.17
96.73
93.37
9 6". 79
79.62
Average
C4 %
98.23
97.82
95.40
94.27
84.97
77.52
96.82
95.95
97.85
96.81
95.46
95.99
92.72
96.07
79.61
Rec.
99.
98.
96.
95.
85.
78.
98.
97.
98.
97.
96.
96.
93.
96.
79.
54
83
64
34
88
85
17
45
83
80
70
97
59
93
70
Average Desorption Efficiencies (percent)
MEK
ETHYLACETATE
2-BUTANOL
N-BUTANOL
METHOXYACETONE
ETHOXYETHANOL
MIBK1
TOLUENE
BUTYLACETATE
ETHYLBENZENE
M & P XYLENE
PMGE ACETATE
O-XYLENE
2-EOE ACETATE
2-MOE ETHER
Level 1
104.64
103.01
100.67
93.16
49.02
22.29
103.43
102.46
104.11
104.59
120.48
103.97
101.18
104.74
68.22
Level 2
98.61
97.79
95.11
93.36
80.16
63.54
96.82
96.33
97.68
97.23
97.78
95.94
93.07
95.89
73.50
Level 3
99.54
98.83
96.64
95.34
85.88
78.85
98.17
97.45
98.83
97.80
96.70
96.97
93.59
96.93
79.70
Average
100.93
99.88
97.48
93.95
71.69
54.89
99.47
98.74
100.21
99.87
104.98
98.96
95.94
99.19
73.81
28
-------
Page 4
MID-PACIFIC ENVIRONMENTAL LABORATORY
Instrument ID: 3400-2 (DB624 60m column)
Date: 4/25/91
MDL Study (4/25/91)
MEK
ETHYLACETATE
2-BUTANOL
N-BUTANOL
METHOXYACETONE
ETHOXYETHANOL
MIBK1
TOLUENE
BUTYLACETATE
ETHYLBENZENE
M & P XYLENE
PMGE ACETATE
0-XYLENE
2-EOE ACETATE
2-MOE ETHER
Al
38.78
36.27
38.61
30.90
9.38
5.98
32.43
35.21
27.34
35.96
33.48
39.90
35.41
40.64
25.33
A2
38.69
36.24
37.92
30.56
9.33
6.05
32.11
34.89
27.08
35.63
45.82
39.70
35.51
40.37
26.28
A3
38.85
36.15
38.52
30.80
9.14
6.69
32.09
34.85
27.05
35.47
40.61
39.34
35.50
38.28
26.98
A4
38.55
35.54
37.97
30.70
9.41
6.25
31.63
34.38
26.80
35.18
43.94
39.10
35.23
39.91
25.11
AS
38.45
35.31
37.42
30.17
8.94
6.04
31.44
34.15
26.49
34.75
40.38
38.74
34.62
37.61
25.48
A6
37.75
35.03
37.10
29.92
9.38
7.20
30.88
33.54
26.16
34.20
42.09
38.29
34.29
37.28
27.16
Ex
A7
37.66
35.17
37.08
29.70
9.17
6.50
30.95
33.69
26.17
34.26
44.29
38. '33
34.34
38.98
26.08
tract
cone.
37.00
35.00
38.00
33.00
19.00
28.00
31.00
34.00
26.00
34.00
34.00
38.00
35.00
38.00
38.00
Mean
(ug/mL)
38.39
35.67
37.80
30.39
9.25
6.38
31.65
34.39
26.73
35.06
41.52
39.06
34.98
39.01
26.06
STD 1
(n-1)
0.49
0.54
0.63
0.47
0.17
0.44
0.60
0.63
0.47
0.68
4.06
0.63
0.55
1.34
0.80
Bxt. MDL
(ug/mL)
1.53
1.68
1.97
1.46
0.54
1.40
1.87
1.99
1.47
2.14
12.76*
1.99
1.73
4.22
2.52
RDL
(ug/ml)
5
5
5
5
10
10
5
2
5
2
2
5
2
10
10
RDL
(ug/tube)
20
20
20
20
40
40
20
8
20
8
8
20
8
40
40
* Bad calibration curve for M&P-Xylene.
RDL " Reporting limit based on instrument sensitivity and MDL study.
-------
APPENDIX F
REDUCED DATA FOR THE BASELINE TEST SERIES
30
-------
Travfs AFB
Date:
Start Tine:
Stop Time:
Organics
18 April, 1991
17:17
18:22
Booth: STP
T= 67.7 P=29.92 "Hg
P= 29.88 T=68 "F
U
I
I
Site Location | Date
1 |18 April
2 |18 April
3 |18 April
4 | 18 April
5 (18 April
6 |1B April
7 (18 April
8 |18 April
9 | 18 April
10 |18 April
11 |18 April
12 | 18 April
13 |18 April
U |18 April
15 | 18 April
16 | 18 April
17 |18 April
18 |1B April
19 |18 April
20 | 18 April
21 |18 April
22 |18 April
23 |18 April
24 | 18 April
1
(Duplicate) 10 |18 April
(Duplicate) 15 |18 April
Painter UM |18 April
Painter OH | 18 April
Blank |1B April
Sample
Number
67
62
47
52
65
44
57
55
49
64
46
50
42
59
45
51
68
41
58
56
53
60
69
48
61
63
66
54
71
Time
Sampled
(min)
0.00
66.00
0.00
76.00
78.00
77.00
77.00
60.00
78.00
0.00
76.00
45.00
3.00
77.00
76.00
75.00
77.00
77.00
76.00
75.00
78.00
77.00
76.00
75.00
77.00
77.00
81.00
81.00
0.00
Sample
Flowrate
(1 /min)
1.633
1.315
1.468
1.371
1.399
1.426
1.371
.381
.012
.018
.313
.284
.355
1.35
0.956
1.369
1.331
.317
.098
.322
.309
.319
.318
.276
.0.927
0.905
1.298
1.285
0
Volume
Collected
(I)
0.00
. 86.79
0.00
104.20
109.12
109.80
105.57
82.86
78.94
0.00
99.79
57.78
4.07
103.95
72.66
102.68
102.49
101.41
83.45
99.15
102.10
101.56
100.17
95.70
71.38
69.69
105.14
104.09
0.00
Volume
Collected | 2-Butanone (KEK)
aCTD 1 •....-._.....- ...
(I) | (ug/tube) (mg/m3)
0.00 x < 20 < N/A
86.72 x 48 0.553484
0.00 x < 20 < NJ/A
104.12 x 27 0.259326
109.04 x 160 1.467376
109.72 x 120 1.093717
105.49 x 39 0.369717
82.80 x 29 0.350257
78.88 x 680 8.621201
0.00 x 57 N/A
99.71 x 83 0.832403
57.74 x 65 1.125822
4.06 x 140 34.46684
103.87 x 1100 10.59015
72.60 x 160 2.203852
102.60 x 170 1.656983
102.41 x 1500 14.64726
101.33 x 1800 17.76356
83.38 x 350 4.197455
99.07 x < 20 < 0.201869
102.02 x 1100 10.78182
101.48 x 540 5.320987
100.09 x 140 1.398727
95.63 x 120 1.254883
71.32 x 200 2.804100
69.63 x 160 2.297813
105.06 x 30 0.285558
104.00 x 5300 50.95909
0.00 x < 20 < N/A
Ethyl Acetate
(ug/tube) (mg/m3)
20 < N/A
< 20 < 0.230618
20 < N/A
< 20 < 0.192093
< 20 < 0.183422
< 20 < 0.182286
< 20 < 0.189598
<• 20 < 0.241556
< 20 < 0.253564
20 < N/A
< 20 < 0.200579
< 20 < 0.346406
< 20 < 4.923834
< 20 < 0.192548
< 20 < 0.275481
< 20 < 0.194939
< 20 < 0.195296
< 20 < 0.197372
< 20 < 0.239854
< 20 < 0.201869
< 20 < 0.196033
< 20 < 0.197073
< 20 < 0.199818
< 20 < 0.209147
< 20 < 0.280410
< 20 < 0.287226
< 20 < 0.190372
< 20 < 0.192298
20 < V/A
2-Butanol
(ug/tube) (mg/m3)
21 < N/A
< 21 < 0.242149
21 < N/A
< 21 < 0.201698
< 21 < 0.192593
< 21 < 0.191400
< 21 < 0.199078
< 21 < 0.253634
< 21 < 0.266242
21 < N/A
< 21 < 0.210608
< 21 < 0.363727
< 21 < 5.170026
< 21 < 0.202175
< 21 < 0.289255
< 21 < 0.204686
< 21 < 0.205061
< 21 < 0.207241
< 21 < 0.251847
< 21 < 0.211963
< 21 < 0.205834
< 21 < 0.206927
< 21 < 0.209809
< 21 < 0.219604
< 21 < 0.294430
< 21 < 0.301587
< 21 < 0.199891
< 21 < 0.201913
21 < N/A.
n-Butanol
(ug/tube) (mg/m3)
21 < f//A
< 21 < 0.242149
21 < fy/A
< 21 < 0.201698
< 21 < 0.192593
< 21 < 0.191400
< 21 < 0.199078
< 21 < 0.253634
< 21 < 0.266242
21 < IV/A
< 21 < 0.210608
< 21 < 0.363727
< 21 < 5.170026
< 21 < 0.202175
< 21 < 0.289255
< 21 < 0.204686
< 21 < 0.205061
< 21 < 0.207241
< 21 < 0.251847
< 21 < 0.211963
< 21 < 0.205834
< 21 < 0.206927
< 21 < 0.209809
< 21 < 0.219604
< 21 < 0.294430
< 21 < 0.301587
< 21 < 0.199891
< 21 < 0.201913
< 21 < 'N/A
Painter UH = Underneath painter respirator hood
Painter OH = Outside painter respirator hood.
-------
Travis AF8
Date: IS April, 1991
Start Time: 17:17
Stop Time: 18:22
1
Site Location | Date
1 |18 April
2 |18 April
3 (18 April
4 | 18 April
5 |18 April
6 | 18 April
7 | 18 April
8 | 18 April
9 |18 April
10 | 18 April
11 |18 April
12 |18 April
13 |18 April
14 |18 April
15 |18 April
16 | 18 April
17 |18 April
18 | 18 April
19 | 18 April
20 |18 April
21 | 18 April
22 | 18 April
23 | 18 April
24 | 18 April
(Duplicate) 10 |18 April
(Duplicate) 15 |18 April
Painter UH |18 April
Painter OH |18 April
Blank | 18 April
Sample
Nuitoer
67
62
47
52
65
44
57
55
49
64
46
50
42
59
45
51
68
41
58
56
53
60
69
48
61
63
66
54
71
Hethoxyacetone
(ug/tube) (mg/m3)
< 56 < N/A
< 56 < 0.645732
56 « IV/A
< 56 < 0.537862
< 56 < 0.513581
< 56 < 0.510401
< 56 < 0.530876
< 56 < 0.676358
< 56 < 0.709981
56 < N/A
< 56 < 0.561621
< 56 < 0.969939
< 56 < 13.78673
< 56 < 0.539135
< 56 < 0.771348
< 56 < 0.545829
< 56 < 0.546831
< 56 < 0.552644
< 56 < 0.671592
< 56 < 0.565235
< 56 < 0.548893
< 56 < 0.551806
< 56 < 0.559490
< 56 < 0.585612
< 56 < 0.785148
< 56 < 0.804234
< 56 < 0.533043
< 56 < 0.538435
56 < N/A
Ethoxyethanol
(ug/tube) (mg/m3>
73 < N/A
< 73 < 0.841757
73 < (V/A
< 73 < 0.701141
< 73 < 0.669490
< 73 < 0.665344
< 73 < 0.692036
< 73 < 0.881681
< 73 < 0.925511
73 < N/A
400 4.011582
< 73 < 1.264385
< 73 < 17.97199
< 73 < 0.702801
< 73 < 1.005507
< 73 < 0.711528
< 73 < 0.712833
< 73 < 0.720411
< 73 < 0.875469
< 73 < 0.736824
< 73 < 0.715521
< 73 < 0.719318
< 73 < 0.729336
< 73 < 0.763387
< 73 < 1.023496
< 73 < 1.048377
< 73 < 0.694859
< 73 < 0.701889
73 < N/A
4-Hethyl-2-Pentanone(MIBK)
(ug/tube) (mg/m3)
< 20 < N/A
< 20 < 0.230618
20 « N/A
75 0.720351
< 20 < 0.183422
< 20 < 0.182286
130 1.232392
110 1.328561
84 1.064971
20 < N/A
50 0.501447
300 5.196102
120 29.54300
350 3.369593
890 12.25892
980 9.552023
550 5.370663
1000 9.868644
1600 19.18836
< 20 < 0.201869
170 1.666282
150 1.478052
760 7.593090
620 6.483563
52 0.729066
850 12.20713
< 20 < 0.190372
1200 11.53790
< 20 < N/A
Toluene
I . ...
(ug/tube) (mg/niS)
8.2 < N/A
< 8.2 < 0.094553
8.2 « N/A
10 0.096046
< 8.2 < 0.075203
< 8.2 < 0.074737
17 0.161159
19 0.229478
< 8.2 < 0.103961
< 8.2 < N/A
100 1.002895
38 0.658173
14 3.446684
35 0.336959
100 1.377407
120 1.169635
58 0.566360
110 1.085550
180 2.158691
< 8.2 < 0.082766
16 0.156826
16 0.157658
91 0.909172
74 0.773844
< 8.2 < 0.114968
100 1.436133
< 8.2 < 0.078052
130 1.249940
8.2 « N/ft
Butyl Acetate
(ug/tube) (mg/m3)
20 < N/A
< 20 < 0.230618
20 < N/A
< 20 < 0.192093
< 20 < 0.183422
< 20 < 0.182286
28 0.265438
31 0.374412
< 20 < 0.253564
20 « N/A
< 20 < 0.200579
80 1.385627
22 5.416218
62 0.596899
230 3.168037
260 2.534210
110 1.074132
230 2.269788
400 4.797092
< 20 < 0.201869
26 0.254843
31 0.305464
200 1 .998181
160 1.673177
< 20 < 0.280410
230 3.303106
< 20 < 0.190372
270 2.596029
20 < N/A
CO
to
Painter UH
Painter OH
= Underneath painter respirator hood.
= Outside painter respirator hood.
-------
Travis AFB
Date: 18 April. 1991
Start Time: 17:17
Stop Time: 18:22
1
1
1
Site Location | Date
1 |18 April
2 | 18 April
3 |18 April
4 |18 April
5 | 18 April
6 | 18 April
7 | 18 April
8 | 18 April
9 | 18 April
10 | 18 April
11 |18 April
12 |18 April
13 |18 April
14 |18 April
15 |18 April
16 |18 April
17 |18 April
18 | 18 April
19 |18 April
20 | 18 April
21 |18 April
22 |18 April
23 |18 April
24 |18 April
1
(Duplicate) 10 |18 April
(Duplicate) 15 |18 April
Painter UH |18 April
Painter OH |18 April
Blank |18 April
Nunfcer
67
62
47
52
65
44
57
55
49
64
46
50
42
59
45
51
68
41
58
56
53
60
69
48
61
63
66
54
71
Ethylbenzene
(ug/tube) (mg/m3)
< 8.2 < N/A
< 8.2 < 0.094553
< 8.2 < IV/A
< 8.2 < 0.078758
< 8.2 < 0.075203
< 8.2 < 0.074737
< 8.2 < 0.077735
< 8.2 < 0.099038
< 8.2 < 0.103941
< 8.2 < N/A
< 8.2 < 0.082237
< 8.2 < 0.142026
< 8.2 < 2.018772
< 8.2 < 0.078944
< 8.2 < 0.112947
< 8.2 < 0.079925
< 8.2 < 0.080071
< 8.2 < 0.080922
< 8.2 < 0.098340
< 8.2 < 0.082766
< 8.2 < 0.080373
< 8.2 < 0.080800
< 8.2 < 0.081925
< 8.2 < 0.085750
< 8.2 < 0.114968
< 8.2 < 0.117762
< 8.2 < 0.078052
< 8.2 < 0.078842
< 8.2 < V/A
Total Xylenes
(ug/tube) (mg/mS)
< 8.2 < fj((\
< 8.2 < 0.094553
< 8.2 < &//A
< 8.2 < 0.078758
< 8.2 < 0.075203
< 8.2 < 0.074737
< 8.2 < 0.077735
< 8.2 < 0.099038
< 8.2 < 0.103961
< 8.2 < ({/A
< 8.2 < 0.082237
< 8.2 < 0.142026
< 8.2 < 2.018772
< 8.2 < 0.078944
< 8.2 < 0.112947
9.6 0.093570
< 8.2 < 0.080071
< 8.2 < 0.080922
< 8.2 < 0.098340
< 8.2 < 0.082766
< 8.2 < 0.080373
< 8.2 < 0.080800
< 8.2 < 0.081925
< 8.2 < 0.085750
< 8.2 < 0.114968
< 8.2 < 0.117762
< 8.2 < 0.078052
9.6 0.092303
< 8.2 < (//A
PMGE Acetate
(ug/tube) (mg/m3)
< 20 < V/A
< 20 < 0.230618
< 20 < (V/A
< 20 < 0.192093
< 20 < 0.183422
< 20 < 0.182286
< 20 < 0.189598
< 20 < 0.241556
< 20 < 0.253564
< 20 < |//A
< 20 < 0.200579
< 20 < 0.346406
< 20 < 4.923834
< 20 < 0.192548
< 20 < 0.275481
< 20 < 0.194939
< 20 < 0.195296
< 20 < 0.197372
< 20 < 0.239854
< 20 < 0.201869
< 20 < 0.196033
< 20 < 0.197073
< 20 < 0.199818
< 20 < 0.209147
< 20 < 0.280410
< 20 < 0.287226
< 20 < 0.190372
< 20 < 0.192298
< 20 < N/fl
2-Ethoxyethyl Acetate
(ug/tube) (mg/m3)
< 41 < WA
< 41 < 0.472768
< 41 < M/A
< 41 < 0.393791
< 41 < 0.376015
< 41 < 0.373686
< 41 < 0.388677
< 41 < 0.495191
< 41 < 0.519807
41 < N/A
< 41 < 0.411187
< 41 < 0.710134
< 41 < 10.09386
< 41 < 0.394723
< 41 < 0.564737
< 41 < 0.399625
< 41 < 0.400358
< 41 < 0.404614
< 41 < 0.491701
82 0.827666
< 41 < 0.401868
< 41 < 0.404000
< 41 < 0.409627
< 41 < 0.428751
< 41 < 0.574840
< 41 < 0.588814
< 41 < 0.390263
< 41 < 0.394211
< 41 < M/A
2-Hethoxyethyl Ether
(ug/tube) (mg/m3)
< 54 < N/A
< 54 < 0.622670
5* < W/A
< 54 < 0.518652
< 54 < 0.495239
< 54 < 0.492172
< 54 < 0.511917
< 54 < 0.652203
< 54 < 0.684624
54 < tf/ft
< 54 < 0.541563
< 54 < 0.935298
< 54 < 13.29435
< 54 < 0.519880
< 54 < 0.743800
< 54 < 0.526335
< 54 < 0.527301
< 54 < 0.532906
< 54 < 0.647607
< 54 < 0.545048
< 54 < 0.529289
< 54 < 0.532098
< 54 < 0.539509
< 54 < 0.564697
< 54 < 0.757107
< 54 < 0.775511
< 54 < 0.514005
< 54 < 0.519205
< 54 < Kf/A
H/A
0.553484
N/A
1.075724
1.467376
1.093717
2.028708
2.282710
9.686173
H/A
2.537325
8.365725
72.87275
14.89360
19.00822
15.00642
21.65842
30.98754
30.34160
0.827666
12.85978
7.262162
11.89917
10.18546
3.533166
19.24418
0.285558
66.34297
Painter UH = Underneath painter respirator hood.
Painter OH = Outside painter respirator hood.
-------
Travis AFB NIOSH
Date: 18 April, 1991
Start Time: 10:02
Stop Time: 11:02
Site Location
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
(Duplicate) 10
(Duplicate) 15
Painter UH
Painter OH
Blank
Date
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 Apr! I
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
Number
24
20
13
31
16
25
28
33
23
19
32
18
26
21
38
27
36
29
35
14
39
22
37
17
12
15
11
34
30
Ethoxyethanol
(ug/tube) (mg/m3)
< 73 < 0.780
< 73 < 0.907
< 73 < 1.937
< 73 < 0.753
< 73 < 0.709
< 73 < 0.713
< 73 < 0.758
< 73 < 0.767
< 73 < 0.899
< 73 < 1.022
< 73 < 0.773
< 73 < 0.806
< 73 < 0.745
< 73 < 0.756
< 73 < 1.097
< 73 < 0.771
< 73 < 0.748
< 73 < 0.765
< 73 < 0.889
< 73 < 0.796
< 73 < 0.751
< 73 < 0.757
< 73 < 0.780
< 73 < 0.797
< 73 < 1.067
< 73 < 1.149
< 73 < 1.265
< 73 < 0.881
< 73 N/A
4-Methyt-2-Pentanone(MlBK)
(ug/tube) (rog/mJ)
< 20 < 0.214
< 20 < 0.248
< 20 < 0.531
160 1.651
< 20 < 0.194
24 0.234
150 1.557
250 2.626
47 0.579
100 1.400
510 5.400
440 4.859
320 3.264
450 4.662
1100 16.527
1400 14.793
300 3.074
930 9.740
** 2300 ** 28.025
2000 21.808
170 1.748
300 3.111
790 8.440
710 7.755
120 1.753
1100 17.319
•* 1700 ** 29.450
< 20 < 0.241
< 20 N/A
Toluene
(ug/tube) (mg/m3)
< 8.2 0.088
< 8.2 0.102
< 8.2 0.218
23 0.237
< 8.2 0.080
< 8.2 0.080
23 0.239
38 0.399
< 8.2 < 0.101
16 0.224
73 0.773
65 0.718
33 0.337
65 0.673
150 2.254
190 2.008
37 0.379
110 1.152
310 3.777
280 3.053
19 0.195
44 0.456
110 1.175
100 1.092
18 0.263
150 2.362
230 3.984
< 8.2 < 0.099
< 8.2 N/A
Butyl Acetate
(ug/tube) (mg/m3)
< 20 < 0.214
< 20 < 0.248
< 20 < 0.531
43 0.444
< 20 < 0.194
< 20 < 0.195
39 0.405
67 0.704
< 20 < 0.246
24 0.336
140 1.482
120 1.325
46 0.469
130 1.347
320 4.808
400 4.227
60 0.615
210 2.199
660 8.042
570 6.215
25 0.257
80 0.830
220 2.350
200 2.185
33 0.482
310 4.881
440 7.622
< . 20 < 0.241
< 20 N/A
Ethylbenzene
(ug/tube) (mg/m3)
8.2 < 0.088
8.2 < 0.102
8.2 < 0.218
8.2 < 0.085
8.2 < 0.080
8.2 < 0.080
< 8.2 < 0.085
< 8.2 < 0.086
< 8.2 < 0.101
< 8.2 < 0.115
< 8.2 < 0.087
< 8.2 < 0.091
< 8.2 < 0.084
< 8.2 < 0.085
< 8.2 < 0.123
< 8.2 < 0.087
< 8.2 < 0.084
< 8.2 < 0.086
< 8.2 < 0.100
< 8.2 < 0.089
< 8.2 < 0.084
< 8.2 < 0.085
< 8.2 < 0.088
< 8.2 < 0.090
< 8.2 < 0.120
< 8.2 < 0.129
< 8.2 < 0.142
< 8.2 < 0.099
< 8.2 N/A
Painter UH = Underneath painter respirator hood.
Painter OH = Outside painter respirator hood.
-------
Travis AFB NIOSH 1300, Organics
Date: 18 April, 1991 Booth: STP
Start Time: 10:02 T=61.3 P*29.92 "Hg
Stop Time: 11:02 P=29.88 T=68 "F
Volume
Site Location
1
2
3
4
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
21
22
23
24
(Duplicate) 10
(Duplicate) IS
Painter UH
Painter OH
Blank
Date
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
IB April
18 April
18 April
18 April
18 April
18 April
18 Apri I
18 April
18 Apr! I
18 AprU
18 April
18 April
18 April
CcWWil A
Time
•* ' —J
ofMnpIC otnr^jicu
Number) (min)
24
20
13
31
16
25
28
33
23
19
32
18
26
21
38
27
36
29
35
U
39
22
37
17
12
15
11
34
30
60.0
61.0
26.0
70.0
73.0
71.0
70.0
69.0
70.0
72.0
71.0
70.0
72.0
71.0
70.0
69.0
72.0
72.0
67.0
69.0
73.0
72.0
70.0
70.0
71.0
69.0
44.0
63.0
0.0
Sample
f lowrate
(l/min)
.543
.305
.433
.369
.394
.426
.361
.364
.147
.981
.315
.279
.346
.344
0.94
.356
1.34
.311
.211
.314
.317
.324
.322
.293
0.953
0.91
1.297
1.3
0
Collected
aCTD
air
(i)
93.6
80.5
37.7
96.9
102.9
102.4
96.4
2-Butanone (MEK)
(ug/tube) (rag/nfl)
< 20 < 0.214
< 20 < 0.248
< 20 < 0.531
38 0.392
65 0.631
28 0.273
44 0.457
95.2 x 61 0.641
81.2 x 350 4.310
71.4 x 70 0.980
94.4 x 110 1.165
90.6 x 82 0.905
98.0 x" 1900 ** 19.382
96.5 x 530 5.491
66.6 x 210 3.155
94.6 x 270 2.853
97.6 x 2100 21.519
95.5 x 1400 14.663
82.1 x 540 6.580
91.7 x 430 4.689
97.2 x 920 9.460
96.4 x 190 1.970
93.6 x 180 1.923
91.6 x 150 1.638
68.4 x 140 2.046
63.5 x 200 3.149
57.7 x 1000 17.324
82.8 x < 20 < 0.241
0.0 x < 20 N/A
Ethyl Acetate
(ug/tube) (mg/m3)
< 20 < 0.214
< 20 < 0.248
< 20 < 0.531
< 20 < 0.206
< 20 < 0.194
< 20 < 0.195
< 20 < 0.208
< 20 < 0.210
< 20 < 0.246
< 20 < 0.280
< 20 < 0.212
< 20 < 0.221
< 20 < 0.204
< 20 < 0.207
< 20 < 0.300
< 20 < 0.211
< 20 < 0.205
< 20 < 0.209
< 20 < 0.244
< 20 < 0.218
< 20 < 0.206
< 20 < 0.207
< 20 < 0.214
< 20 < 0.218
110 1.607
< 20 < 0.315
< 20 < 0.346
< 20 < 0.241
< 20 N/A
2-Butanol
(ug/tube) (mg/m3)
< 21 < 0.224
< 21 < 0.261
< 21 < 0.557
< 21 < 0.217
< 21 < 0.204
< 21 < 0.205
< 21 < 0.218
< 21 < 0.221
< 21 < 0.259
< 21 < 0.294
< 21 < 0.222
< 21 < 0.232
< 21 < 0.214
< 21 < 0.218
< 21 < 0.316
< 21 < 0.222
< 21 < 0.215
< 21 < 0.220
< 21 < 0.256
< 21 < 0.229
< 21 < 0.216
< 21 < 0.218
< 21 < 0.224
< 21 < 0.229
< 21 < 0.307
< 21 < 0.331
< 21 < 0.364
< 21 < 0.253
< 21 N/A
n- Butane I
(ug/tube) (mg/m3)
< 21 < 0.224
< 21 < 0.261
< 21 < 0.557
< 21 < 0.217
< 21 < 0.204
< 21 < 0.205
< 21 < 0.218
< 21 < 0.221
< 21 < 0.259
< 21 < 0.294
< 21 < 0.222
< 21 < 0.232
< 21 < 0.214
< 21 < 0.218
< 21 < 0.316
< 21 < 0.222
< 21 < 0.215
< 21 < 0.220
< 21 < 0.256
< 21 < 0.229
< 21 < 0.216
< 21 < 0.218
< 21 < 0.224
< 21 < 0.229
< 21 < 0.307
< 21 < 0.331
< 21 < 0.364
< 21 < 0.253
< 21 N/A
Methoxyacetone
(ug/tube) (mg/m3)
< 56 < 0.598
< 56 < 0.695
< 56 < 1.486
< 56 < 0.578
< 56 < 0.544
< 56 < 0.547
< 56 < 0.581
< 56 < 0.588
< 56 < 0.690
< 56 < 0.784
< 56 < 0.593
< 56 < 0.618
< 56 < 0.571
< 56 < 0.580
< 56 < 0.841
< 56 < 0.592
< 56 < 0.574
< 56 < 0.587
< 56 < 0.682
< 56 < 0.611
< 56 < 0.576
< 56 < 0.581
< 56 < 0.598
< 56 < 0.612
< 56 < 0.816
< 56 < 0.882
< 56 < 0.970
< 56 < 0.676
< 56 N/A
Painter UH = Underneath painter resnirator hood.
Painter OH = Outside painter respirator hood.
-------
Travis AFB NIOSH
Date: 18 April, 1991
Start Time: 10:02
Stop Time: 11:02
Site Location
Date
Nunfcer
Total Xylenes
(ug/tube) (mg/m3)
PHGE Acetate
(ug/tube) (mg/m3)
2-Ethoxyethyl Acetate
(ug/tube) (mg/mj)
2-Methoxyethyl Ether
(ug/tube) (mg/m3)
Totals
(mg/m3)
CO
O)
1
2
3
4
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
21
22
23
24
(Duplicate) 10
(Duplicate) 15
Painter UH
Painter OH
Blank
18 April
18 April
18 April
18 April
18 April
18 April
18 Apri I
18 April
18 April
18 April
18 April
18 April
18 Apri I
18 April
18 April
18 Apri I
18 April
18 Apr! I
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
18 April
24
20
13
31
16
25
28
33
23
19
32
18
26
21
38
27
36
29
35
U
39
22
37
17
12
15
11
34
30
< 8.2 < 0.088
< 8.2 < 0.102
< 8.2 < 0.218
< 8.2 < 0.085
< 8.2 < 0.080
< 8.2 < 0.080
< 8.2 < 0.085
< 8.2 < 0.086
< 8.2 < 0.101
< 8.2 < 0.115
< 8.2 < 0.087
< 8.2 < 0.091
< 8.2 < 0.084
< 8.2 < 0.085
16 0.240
20 0.211
< 8.2 < 0.084
9.9 0.104
33 0.402
29 0.316
< 8.2 < 0.084
< 8.2 < 0.085
10 0.107
< 8.2 < 0.090
< 8.2 < 0.120
16 0.252
15 0.260
< 8.2 < 0.099
< 8.2 N/A
< 20 0.214
< 20 0.248
< 20 0.531
< 20 0.206
< 20 0.194
< 20 0.195
< 20 0.208
< 20 0.210
< 20 0.246
< 20 0.280
* 20 0.212
< 20 0.221
< 20 0.204
< 20 0.207
< 20 0.300
< 20 0.211
< 20 0.205
< 20 0.209
< 20 < 0.244
< 20 < 0.218
< 20 < 0.206
< 20 < 0.207
< 20 < 0.214
< 20 < 0.218
< 20 < 0.292
< 20 < 0.315
< 20 < 0.346
< 20 < 0.241
< 20 N/A
< 41 < 0.438
< 41 < 0.509
< 41 < 1.088
< 41 < 0.423
< 41 < 0.398
< 41 < 0.400
< 41 < 0.425
< 41 < 0.431
< 41 < 0.505
< 41 < 0.574
< 41 < 0.434
< .41 < 0.453
< 41 < 0.418
< 41 < 0.425
< 41 0.616
< 41 0.433
41 0.420
41 0.429
41 0.500
41 < 0.447
41 < 0.422
41 < 0.425
41 < 0.438
< 41 < 0.448
< 41 < 0.599
< 41 < 0.646
< 41 < 0.710
< 41 < 0.495
< 41 N/A
< 54 < 0.577
< 54 < 0.671
< 54 < 1.433
< 54 < 0.557
< 54 < 0.525
< 54 < 0.527
< 54 < 0.560
< 54 < 0.567
< 54 < 0.665
< 54 < 0.756
< 54 < 0.572
< 54 < 0.596
< 54 < 0.551
< 54 < 0.559
< 54 < 0.811
< 54 < 0.571
< 54 < 0.553
< 54 < 0.566
< 54 < 0.658
< 54 < 0.589
< 54 < 0.555
< 54 < 0.560
< 54 < 0.577
< 54 < 0.590
< 54 < 0.789
< 54 < 0.850
< 54 < 0.935
< 54 < 0.652
< 54 N/A
< 4.171059
< 4.850909
< 10.36439
2.723539
0.631479
0.507758
2.656532
4.369796
5.134591
2.939335
8.820479
7.806963
23.45269
12.17339
26.98433
24.09114
25.58659
27.85873
46.82553
36.08141
11.66099
6.367650
13.99500
12.67047
6.151232
27.96300
58.64045
< 0.823250
N/A
Painter UH = Underneath painter respirator hood.
Painter OH = Outside painter respirator hood.
-------
1 1
1 1
1 1
| Site Location | Date
1 1
(Exhaust Duct, 10:30 |16 April
(Exhaust Duct, 14:45 (16 April
(Exhaust Duct, Blank |17 April
(Exhaust Duct, 10:00 (17 April
(Exhaust Duct, 16:00 (17 April
(Exhaust Duct ,4pm Dup| 17 April
(Exhaust Duct, 11:00 (18 April
(Exhaust Duct, 17:00 (18 April
(Exhaust Duct, 11:30 (19 April
(Exhaust Duct. 15:00 (19 April
Conwtl A APIIDCV #
bafnpie ALUKcX W
Number
5F 12993
9F 7996
7F 9995
8F 7995
10F 12994
6F 10994
40F 8383
70F 12015
75F 11050
74F . 12995
Time | Sample Sample
_ iJIcl * r 1 ..
sampled jriowrate riowrate
(min) |(cc/min) (l/min)
1
36.00 | 1066.00 1.066
54.00 |1067.000 1.067
0.00 | 0.000 0
60.00 (1059.000 .059
60.00 (1089.000 .089
60.00 | 1053.00 .053
53.00 | 1026.00 .026
60.00 (1027.000 .027
53.00 | 991.00 0.991
42.00 | 991.000 0.991
Volume
p—l 1 As»*A>4
col lecteci
CD
38.38
57.62
0.00
63.54
65.34
63.18.
54.38
61.62
52.52
41.62
Volume
Collected
aCTD
5TP
(I)
38.35
57.57
0.00
63.49
65.29
63.13
54.34
61.57
52.48
41.59
Booth: STP
T= 67.7 P=29.92 "
P= 29.88 T=68 °F
2-Butanone (MEK)
(ug/tube) (mg/m3)
57 1 .486446
49 0.851082
20 < N/A
230 3.622552
< 20 < 0.306326
< 20 < 0.316799
78 1 .435507
170 2.760967
230 4.382403
240 5.770617
Hg
Ethyl Acetate
(ug/tube) (mg/m3)
< 20 < 0.521560
< 20 < 0.347380
20 < N/A
< 20 < 0.315004
< 20 < 0.306326
< 20 < 0.316799
< 20 < 0.368078
< 20 < 0.324819
< 20 < 0.381078
< 20 < 0.480884
-------
1
1
Site Location | Date
1
Exhaust Duct, 10:30 |16 April
Exhaust Duct, 14:45 |16 April
Exhaust Duct, Blank |17 April
Exhaust Duct, 10:00 | 17 April
Exhaust Duct, 16:00 |17 April
Exhaust Duct, 4pm Dup|17 April
Exhaust Duct, 11:00 |18 April
Exhaust Duct, 17:00 |18 April
Exhaust Duct, 11:30 |19 April
Exhaust Duct, 15:00 |19 April
2-Butanol
(ug/tube) (mg/m3)
< 21 < 0.547638
< 21 < 0.364749
21 < N/A
< 21 < 0.330754
< 21 < 0.321643
< 21 < 0.332639
< 21 < 0.386482
< 21 < 0.341060
< 21 < 0.400132
< 21 < 0.504929
n-Butanol
(ug/tube)
-------
1
1
1
Site Location | Date
1
Exhaust Duct, 10:30 |16 April
Exhaust Duct. 14:45 |16 April
Exhaust Duct, Blank | 17 April
Exhaust Duct, 10:00 |17 April
Exhaust Duct, 16:00 |17 April
Exhaust Duct, 4pm Dup|17 April
Exhaust Duct, 11:00 |18 April
Exhaust Duct. 17:00 |18 April
Exhaust Duct, 11:30 |19 April
Exhaust Duct, 15:00 |19 April
Toluene
(ug/tube) (mg/m3)
21 0.547638
29 0.503702
< 8.2 < N/A
27 0.425256
10 0.153163
17 0.269279
35 0.644137
21 0.341060
13 0.247701
11 0.264486
Butyl Acetate
(ug/tube) (mg/m3)
< 20 < 0.521560
53 0.920559
< 20 < tf/A
21 0.330754
< 20 < 0.306326
< 20 < 0.316799
61 1.122640
39 0.633398
27 0.514456
24 0.577061
Ethylbenzene
(ug/tube) (mg/m3)
'
< 8.2 < 0.213839
< 8.2 < 0.142426
8.2 < N/A
< 8.2 < 0.129151
< 8.2 < 0.125593
< 8.2 < 0.129887
< 8.2 < 0.150912
< 8.2 < 0.133176
< 8.2 < 0.156242
< 8.2 < 0.197162
Total Xylenes
(ug/tube) (mg/m3)
< 8.2 < 0.213839
< 8.2 < 0.142426
< 8.2 < |\f/A
< 8.2 < 0.129151
< 8.2 < 0.125593
< 8.2 < 0.129887
< 8.2 < 0.150912
< 8.2 < 0.133176
< 8.2 < 0.156242
< 8.2 < 0.197162
PMGE Acetate
(ug/tube) (mg/m3)
< 20 < 0.521560
< 20 < 0.347380
< 20 < N/A
< 20 < 0.315004
< 20 < 0.306326
< 20 < 0.316799
< 20 < 0.368078
< 20 < 0.324819
< 20 < 0.381078
< 20 < 0.480884
-------
1
1
1
Site Location | Date
1
Exhaust Duct, 10:30 |16 April
Exhaust Duct, 14:45 |16 April
Exhaust Duct, Blank |17 April
Exhaust Duct, 10:00 |17 April
Exhaust Duct, 16:00 | 17 April
Exhaust Duct, 4pm Dup|17 April
Exhaust Duct, 11:00 |18 April
Exhaust Duct, 17:00 |18 April
Exhaust Duct, 11:30 |19 April
Exhaust Duct, 15:00 |19 April
2-Ethoxyethyl Acetate
(ug/tube) (mg/nfl)
< 41 < 1.069198
< 41 < 0.712130
< 41 < N/A
< 41 < 0.645759
< 41 < 0.627969
< 41 < 0.649438
< 41 < 0.754561
< 41 < 0.665880
< 41 < 0.781210
< 41 < 0.985813
2-Hethoxyethyl Ether
(ug/tube) (mg/m3)
< 54 < 1.408212
< 54 < 0.937928
54 < N/A
< 54 < 0.850512
< 54 < 0.827082
< 54 < 0.855358
< 54 < 0.993812
< 54 < 0.877013
< 54 < 1.028912
< 54 < 1.298389
Totals
2.04
5.87
N/A
5.84
0.89
1.57
7.44
6.65
7.05
8.68
-------
Participate
Date: 16 April 1
Start Time: 14:48
Stop Time: 15:48
1
1
Site Location | Date
1
1 |16 April
2 |16 April
3 |16 April
4 |16 April
5 |16 April
6 |16 April
7 (16 April
8 1 16 April
9 |16 April
10 |16 April
11 |16 April
12 |16 April
13 |16 April
14 |16 April
15 |16 April
16 |16 April
17 |16 April
18 |16 April
19 |16 April
20 |16 April
21 |16 April
22 |16 April
23 |16 April
24 |16 April
Painter OH (16 April
Painter UH J16 April
(Duplicate) 10 J16 April
(Duplicate) 15 |16 April
Blank |16 April
1
Exhaust Duct |16 April
991
Sampl e
Number
12
15
3
8
11
19
13
14
17
16
18
4
5
9
' 39
33
1
37
27
30
6
2
32
36
25
24
10
35
7
Time
Sampl ed
(min)
65.00
54.00
63.00
62.00
65.00
63.00
64.00
62.00
63.00
63.00
63.00
62.00
63.00
63.00
63.00
62.00
63.00
64.00
63.00
62.00
63.00
63.00
63.00
62.00
0.00
63.00
63.00
0.00
0.00
Sample
Flowrate
(1/min)
3.1
3.02
3.13
3.093
3.094
3.098
2.961
3.133
3.056
3.059
3.033
3.074
3.074
3.068
3.016
3.062
3.079
3.077
3.077
3.098
3.023
3.076
3.054
3.107
3.064
3.086
3.199
3.178
0
1.067
STP
P=29.92 "He
T=68 *F
Volume
Collected
0)
201.50
163.08
197.19
191.77
201.11
195.17
189.50
194.25
192.53
192.72
191.08
. 190.59
193.66
193.28
190.01
189.84
193.98
196.93
193.85
192.08
190.45
193.79
192.40
192.63
0.00
194.42
201.54
0.00
0.00
0.00
1
Volume
Collected
8 STP
(D
'
201.70
163.24
197.38
191.95
201.31
195.37
189.69
194.44
192.72
192.91
191.27
190.78
193.85
193.47
190.20
190.03
194.17
197.12
194.04
192.27
190.64
193.98
192.59
192.82
0.00
194.61
201.74
0.00
• 0.00
0.00
0.00
Weight
Gain
(9)
0.000(6
0.00000
0.00014
0.00000
0.00009
o.ooooo
0.00055
0.00047
0.00021
0.00076
0.00311
0.00118
0.0008
0.00291
0.00691
0.00526
0.0143
0.00662
0.00435
0.00465
0.0002
0.00088
0.00538
0.00201
0.00000
0.00000
0.00068
0.00046
0.00000
Booth:
T=
P=
Weight
Gain
(mg)
0.2
0.0
0.1
0.0
0.1
o.O
0.6
0.5
0.2
0.8
3.1
1.2
0.8
2.9
6.9
5.3
14.3
6.6
4.4
4.7
0.2
0.9
5.4
2.0
0.0
0.0
0.7
0.5
0.0
0.0
0.0
66.6
29.87
(mg/m3)
0.793
0.000
0.709
o.ooo
0.447
o.ooo
2.899
2.417
1.090
3.940
16.260
6.185
4.127
15.041
36.331
27.680
73.648
33.583
22.418
24.185
1.049
4.537
27.935
10.424
N/A
0-000
3.371
m
N/A
Painter OH = Outside painter respirator hood.
Painter UH = Underneath painter respirator hood.
41
-------
Participate
Date: 17 April 1991 STP Booth:
Start Time: 16:05 P=29.92 "Hg T=
Stop Time: 17:18 T=68 *F P=
Volume
| | | Time Sample | Volume (Collected
| j Sample j Sampled j Flowrate | Collected! 8 STP
Site Location j Date JNumberj (min) j (1/min) (1) j (1)
1
1 |17 April
2 j 17 April
3 j 17 April
4 (17 April
5 j 17 April
6 |17 April
7 |17 April
8 |17 April
9 |17 April
10 |17 April
11 |17 April
12 |17 April
13 j 17 April
14 |17 April
15 |17 April
16 |17 April
17 |17 April
18 |17 April
19 |17 April
20 (17 April
21 |17 April
22 |17 April
23 (17 April
24 j 17 April
Painter OH J17 April
Painter UH J17 April
(Duplicate) 10 |17 April
(Duplicate) 15 J17 April
1
Blank |17 April
Exhaust Duct J17 April
40
58
22
34
52
46
29
23
43
59
45
20
31
38
48
49
42
44
41
53
51
55
47
21
50
57
66
54
Exh. Duct Dup (17 April
84.00
70.00
83.00
82.00
84.00
82.00
83.00
82.00
83.00
83.00
82.00
82.00
82.00
82.00
82.00
82.00
83.00
83.00
82.00
82.00
82.00
82.00
82.00
82.00
78.00
78.00
82.00
82.00
0.00
60.00
60.00
3.052 256.37
3.01
3.038
3.102
2.87
3.096
2.964
3.102
3.045
3.039
3.02
3.036
3.041
3.038
2.963
3.043
3.045
3.071
3.048
3.084
3.012
3.062
3.026
3.05
3.008
3.036
3.16
3.144
0
1.053
1.089
210.70
252.15
254.36
241.08
253.87
246.01
254.36
252.74
252.24
247.64
248.95
249.36
249.12
242.97
249.53
252.74
254.89
249.94
252.89
246.98
251.08
248.13
250.10
234.62
236.81
259.12
257.81
0.00
63.18
65.34
256.45
210.77
252.24
254.45
241.16
253.96
246.09
254.45
252.82
252.32
247.72
249.04
249.45
249.20
243.05
249.61
252.82
254.98
250.02
252.97
247.07
251.17
248.21
250.18
234.70
236.89
259.21
257.89
0.00
0.00
63.20
65.36
68
29.93
Weight
Gain
(9)
0.00003
o.ooooo
0.00000
o.ooooo
0.00008
0.00000
0.00000
0.00042
0.00018
o.oooo
0.00095
0.00042
0.00078
0.00179
0.00012
0.00219
0.00218
0.00522
0.00635
0.00357
0.00044
0.00065
0.00115
0.00072
0.00085
0.00000
0.00044
0.0024
Weight |
Gain j
(mg) j (mg/m3)
1
0.0 | 0.117
o.o * 0.000
0.0* 0.000
0.0 * 0.000
0.1 | 0.332
0.0 * 0.000
o.o * o.ooo
0.4 | 1.651
0.2 | 0.712
o.O * o.OOO
1.0 | 3.835
0.4 j 1.687
0.8 | 3.127
1.8 | 7.183
0.1 | 0.494
2.2 | 8.774
2.2 | 8.623
5.2 | 20.472
6.3 j 25.398
3.6 | 14.112
0.4 | 1.781
0.7 | 2.588
1.2 j 4.633
0.7 j 2.878
0.9 | 3.622
0.0 * 0.000
0.4 | 1.697
2.4 j 9.306
o.o I ty/A
o.o | N/A
0.0 | 0
o.o 1 o
Painter OH = Outside painter respirator hood.
Painter UH = Underneath painter respirator hood.
42
-------
Travis AFB NIOSH 7300
Metals
Date: 16 April, 1991 STP Booth:
start Time: 10:45 p=29.92 -Hg T= 6i Painter UH = Underneath painter respirator hood.
stop Time: 11:25 T=68 °f p= 29.87 Painter OH = Outside painter respirator hood.
Volume
| | | Time Sample Volume (Collected)
| |Sample|Sampled |Flourate|Collected| a STP
Site Location) Date (Number) (min) |(l/min) | (I) (I)
1 1
1 | 16 April) 9
2 | 16 April) 26
3 | 16 April) 43
4 | 16 April) 32
5 |16 April) 40
6 1 16 April) 34
7 |16 April) 35
8 (16 April) 30
9 |16 April) 49
10 | 16 April) 38
11 (16 April) 65
12 (16 April) 25
13 (16 April) 8
14 |16 April) 44
15 |16 April) 24
16 (16 April) 39
17 |16 April) 10
18 (16 April) 61
19 |16 April) 45
20 |16 April) 27
21 |16 April) 69
22 |16 April) 42
23 1 1(5 April) 67
24 |16 April) 41
(Duplicate) 10 | 16 April) 48
(Duplicate)15|16 April) 1
Painter UH |16 April) 28
Painter OH | 16 April) 33
Blank | 16 April) 7
Exhaust Duct |16 April)
1
52.00
46.00
52.00
56.00
53.00
54.00
53.00
59.00
51.00
54.00
51.00
58.00
52.00
53.00
56.00
58.00
52.00
54.00
56.00
59.00
48.00
54.00
56.00
58.00
53.00
52.00
36.00
31.00
0.00
36.00
3.075
2.983
3.025
3.062
3.109
3.085
2.957
3.044
2.998
2.975
2.968
3.009
3.001
2.989
2.91
2.969
3.015
2.993
3.018
3.035
2.981
3.018
3.033
3.054
3.177
3.126
3.022
2.993
0
1.055
159.90
137.22
157.30
171.47
164.78
166.59
156.72
179.60
152.90
160.65
151.37
174.52
156.05
158.42
162.96
172.20
156.78
161.62
169.01
179.07
143.09
162.97
169.85
177.13
168.38
162.55
108.79
92.78
0.00
161.78
138.83
159.15
173.49
166.71
168.55
158.56
181.71
154.69
162.54
153.15
176.57
157.89
160.28
164.87
174.23
158.62
163.52
170.99
181.17
144.77
164.89
171.84
179.21
170.36
164.46
110.07
93.87
0.00
; 111
1
Lead
ug/sample ug/m3
< 1.5 < 9.27
< 1.5 < 10,80
< 1.5 < 9,43
< 1.5 < 8.65
< 1.5 < 9.00
< 1.5 < 8.90
< 1.5 < 9.46
< 1.5 < 8.26
< 1.5 < 9.70
< 1.5 < 9.23
< 1.5 < 9.79
< 1.5 < 8.50
< 1.5 < 9.50
< 1.5 < 9.36
< 1.5 < 9.10
< 1.5 < 8.61
< 1.5 < 9.46
< 1.5 < 9.17
< 1.5 < 8.77
< 1.5 < 8.28
< 1.5 < 10.36
< 1.5 < 9.10
< 1.5 < 8.73
< 1.5 < 8.37
< 1.5 < 8.80
< 1.5 < 9.12
< 1.5 < 13.63
< 1.5 < 15.98
< 1-5 < H/A
-------
Travis AFB NIOSH 7300 Metals
Date: 17 April, 1991 STP Booth:
start rime: 10:03 p=29.92 »Hg T= 60.7 Painter UH = Underneath painter respirator hood.
stop Time: 11:59 T=68 °F p= 29.77 Painter OH = Outside painter respirator hood.
Volume
| | | Time | Sample | Volume (Collected)
| | Sample | Sampled |Flowrate|Collected| a STP
Site Location) Date (Number) (min) |(l/nin) | (I) | (I)
I I
1 |17 April) 56
2 |17 April) 52
3 |17 April) 5
4 |17 April) 22
5 |17 April) 53
6 |17 April) 51
7 |17 April) 46
8 |17 April) 47
9 |17 April) 54
10 |17 April) 20
11 | 17 April) 62
12 | 17 April | 12
13 |17 April) 57
14 |17 April) 31
15 | 17 April) 50
16 |17 April) 18
17 |17 April) 59
18 |17 April) 13
19 |17 April) 70
20 |17 April) 63
21 |17 April) 60
22 |17 April) 19
23 | 17 April) 66
24 |17 April) 4
(Duplicate)10|17 April) 11
(Duplicate)15| 17 April) 64
Painter UH |17 April) 7
Painter OH |17 April) 21
Blank | 17 April) 17
Exhaust Duct |17 April) Bf
I 1
77.00
75.00
74.00
72.00
77.00
74.00
74.00
72.00
75.00
74.00
73.00
71.00
74.00
74.00
73.00
71.00
75.00
74.00
73.00
71.00
75.00
75.00
73.00
72.00
74.00
72.00
31.00
66.00
0.00
60.00
3.11
3.015
3.091
3.117
2.756
3.136
2.981
3.106
3.06
3.051
3.032
3.041
3.053
3.042
2.973
3.048
3.051
3.07
3.089
3.186
3.009
3.077
3.045
3.066
3.186
3.14
3.068
3.054
0
1.059
239.47
226.13
228.73
224.42
212.21
232.06
220.59
223.63
229.50
225.77
221.34
215.91
225.92
225.11
217.03
216.41
228.83
227.18
225.50
226.21
225.68
230.78
222.29
220.75
235.76
226.08
95.11
201.56
0.00
63.54
241.61
228.15
230.78
226.43
214.11
234.14
222.57
225.63
231.55
227.79
223.32
217.84
227.94
227.12
218.97
218.34
230.87
229.21
227.51
228.23
227.69
232.84
224.27
222.73
237.87
228.10
95.96
203.37
0.00
64.11
Lead
ug/sample ug/mj
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
.5 < 6.21
.5 < 6.57
.5 < 6.50
.5 < 6.62
.5 < 7.01
.5 < 6.41
.5 < 6.74
.5 < 6.65
.5 < 6.48
.5 < 6.58
.5 < 6.72
.5 < 6.89
.5 < 6.58
.5 < 6.60
.5 < 6.85
.5 < 6.87
.5 < 6.50
.5 < 6.54
.5 < 6.59
.5 < 6.57
.5 < 6.59
.5 < 6.44
.5 < 6.69
.5 < 6.73
.5 < 6.31
.5 < 6.58
.5 < 15.63
.5 < 7.38
•5 < tf/A
<* 4.7
Zinc
ug/sample ug/m3
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
'<
<
<
<
<
<
<
<
<
<
.5 < 6.21
.5 < 6.57
.5 < 6.50
.5 < 6.62
.5 < 7.01
.5 < 6.41
.5 < 6.74
.5 < 6.65
.5 < 6.48
.5 < 6.58
.5 < 6.72
.5 < 6.89
.5 < 6.58
.5 < 6.60
.5 < 6.85
.5 < 6.87
.5 < 6.50
.5 < 6.54
.5 < 6.59
.5 < 6.57
.5 < 6.59
.5 < 6.44
.5 < 6.69
.5 < 6.73
.5 < 6.31
.5 < 6.58
.5 < 15.63
< 1.5 < 7.38
< 1.5 < N(f\
<1 t>*7
Strontium
ug/sample ug/m3
0.95 3.93
1.92 8.42
3.02 13.09
2.18 9.63
3.51 16.39
1.82 7.77
7.67 34.46
8.40 37.23
5.10 22.03
1.22 5.36
29.63 132.68
26.76 122.84
16.73 73.40
27.56 121.34
112.20 512.40
- 67.98 311.34
53.16 230.26
115.30 503.03
156.32 687.08
54.98 240.90
10,11 44.40
11.54 49.56
63.47 283.00
36.35 163.20
6.02 25.31
92.69 406.35
31.44 327.64
0.78 3.84
1.23 ff/A
m-1 ss:;
Chromium
ug/sample ug/m3
0.33 1.37
0.54 2.37
1.41 6.11
1.17 5.17
0.99 4.62
1.04 4.44
3.72 16.71
4.58 20.30
1.95 8.42
1.50 6.58
14.36 64.30
13.02 59.77
7.91 34.70
14.42 63.49
63.06 287.98
38.13 174.63
29.33 127.04
59.76 260.72
77.64 341.25
29.33 128.51
5.19 22.79
6.06 26.03
35.06 156.33
20.15 90.47
3.65 15.34
53.01 232.40
16.14 168.20
0.15 0.74
0.30 Nffl
75,07 l{
-------
Travis AFB Isocyanates
Date: 19 April. 1991
Start Time: 11:26 Booth: STP:
Stop Time: 12:26 T= 64.3 P=29.92 "Hg
P= 29.8 T=68 *F
Volume
| Time Sample Volume | Collected] HMD I HHDI
| (Sample (SampledJFlowrate |Collected| 9 STP (per Filter|Concentration|
Site Location j Date | Number (min) j (1/min) (1) | (1) (ug) (ug/m3) j
1
1 |19 April
2 |19 April
3 |19 April
4 |19 April
5 |19 April
6 |19 April
7 j 19 April
8 |19 April
9 j 19 April
10 j 19 April
11 1 19 April
12 |19 April
13 |19 April
14 j 19 April
15 j 19 April
16 |19 April
17 j 19 April
18 j 19 April
19 1 19 April
20 |19 April
21 j 19 April
8
6
2
4
20
14
7
13
22
23
51
43
15
5
59
58
34
18
19
9
21
22 j 19 April 25
23 j 19 April 1
24 j 19 April 35
Exhaust Duct J19 April 10
(Duplicate) 10 J19 April 11
(Duplicate) 15 |I9 April 24
Painter UH |19 April 54
Painter OH J19 April 41
Blank |19 April 16
1
Exhaust Duct |19 April Tube
66.0
55.0
65.0
64.0
66.0
64.0
64.0
61.0
65.0
64.0
64.0
63.0
65.0
64.0
64.0
63.0
65.0
64.0
64.0
63.0
• 65.0
64.0
64.0
63.0
55.0
64.0
64.0
65.0
65.0
0.0
53.0
3.082
3.314
3.048
3.115
3.069
3.144
3.015
3.094
3.160
3.069
3.158
3.112
3.125
3.149
3.167
3.119
3.136
3.120
3.131
3.162
3.120
3.151
3.118
3.136
3.172
3.127
3.156
3.116
3.106
N/A
0.991
203
182
198
199
203
201
193
189
205
196
202
19.6
203
202
203
196
204
200
200
199
203
202
200
198
174
200
202
203
202
N/A
205
183
199
200
204
202 -
194
190
207
198
203
197
204
203
204
198
205
201
202
200
204
203
201
199
175
201
203
204
203
N/A
53 | 53
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
1.3
1.0
< 1.0
1.5
2.5
2.2
< 1.0
< 1.0
< 1.0
< .0
< .0
< .0
.6
< .0
< 1.0
< 1.0
< 4.9
< 5.5
< 5.0
< 5.0
< 4.9
< 4.9
< 5.2
< 5.3
< 4.8
< 5.1
< 4.9
< 5.1
< 4.9
< 4.9
6.4
5.1
< 4.9
7.5
12.4
11.0
< 4.9
< 4.9
< 5.0
< 5.0
< 5.7
< 5.0
7.9
< 4.9
< 4.9
N/A
Painter UH = Underneath painter respirator hood.
Painter OH = Outside painter respirator hood.
45
-------
Travis AFB Isocyanates
Date: 19 April, 1991
Start Time: 15:15 Booth: STP
Stop Time: 16:00 T= 65.6 P=29.92 "Hg
P= 29.88 T=68 'F
Volume
1
1
Site Location | Date
1
1 |19 April
2 j 19 April
3 |19 April
4 j 19 April
5 j 19 April
6 |19 April
7 j 19 April
8 j 19 April
9 j 19 April
10 |19 April
11 |19 April
12 |19 April
13 J19 April
14 j 19 April
15 j 19 April
16 j 19 April
17 |19 April
18 j 19 April
19 |19 April
20 j 19 April
21 j 19 April
22 |19 April
23 |19 April
24 j 19 April
Exhaust Duct J19 April
Exh. Duct Dup. |19 April
Exh. Duct Blnk J19 April
(Duplicate) 10 |19 April
(Duplicate) 15 J19 April
Painter UH J19 April
Painter OH |19 April
Blank J19 April
1
Time Sample Volume | Collected) HHDI | HMD I
Sample ISampledJFlowrate j Collected! 8 STP
Number (min) (1/min) (1) j (1)
26
17
29
39
45
57
53
31
46
48
30
37
12
47
32
33
38
42
40
52
3
55
28
49
36
44
27
70
50
72
71
56
49.0
40.0
47.0
46.0
48.0
47.0
47.0
45.0
48.0
47.0
47.0
46:0
47.0
47.0
46.0
46.0
47.0
47.0
47.0
45.0
47.0
47.0
46.0
46.0
42.0
42.0
42.0
47.0
46.0
48.0
48.0
0.0
Exhaust Duct |19 April | Charcoal | 42.0
| | Tube |
3.105
3.341
3.012
. 3.041
3.057
3.133
3.019
3.103
3.132
3.044
3.035
3.116
3.118
3.143
3.176
3.155
3.128
3.133
3.120
3.159
3.109
3.150
3.131
3.128
3.159
3.129
N/A
3.130
3.168
3.098
3.185
N/A
0.991
152
134
142
140
147
147
142
140
150
143
143
143
147
148
146
145
147
147
147
142
146
148
144
144
133
131
N/A
147
146
149
153
N/A
42
153
134
142
140
147
148
142
140
151
144
143
144
147
148
147
146
147
148
147
143
147
149
144
144
133
132
N/A
148
146
149
153
N/A
42
per Filter (Concentration)
(ug) | (ug/m3)
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
« 1.0
< 1.0
1.2
< 1.0
< 1.0
< 1.0
2.8
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< 1.0
< liO
1.3
< 1.0
< 1.0
< 1.0
< 6.6
< 7.5
< 7.0
< 7.1
< 6.8
< 6.8
< 7.0
< 7.1
< 6.6
< 7.0
< 7.0
< 7.0
< 6.8
< 6.7
8.2
< 6.9
< 6.8
< 6.8
19.0
< 7.0
< 6.8
< 6.7
< 6.9
< 6.9
< 7.5
< 7.6
N/A
< 6.8
8.9
< 6.7
< 6.5
N/A
Painter UH = Underneath painter respirator hood.
Painter OH = Outside painter respirator hood.
46
-------
APPENDIX G
REDUCED DATA FOR THE POSTMODIFICATION TEST SERIES
47
-------
TEST: ORGANICS #1
DATE: 06-16-92
METHOD: NIOSH 1300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER, GRAY TOPCOAT
OBJECT: AUXILIARY RAMP
PAGE 1 OF 2
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE 1 SAMPLE t PUMP f(ml/min) (ml/mfn) (min)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
2B
3B
TUBE BLN
EXHAUST
RECIRC
15 900433&4
22 900456&5
25 900457&8
24 900469&70
10 900435&6
20 900454&3
14 900459&60
11 900471&2
54 900437&8
5 900451&2
56 900461&2
59 900473&4
18 900439&40
8 900450&49
58 900463&4
29 900475&6
1 900441&2
13 900447&8
28 900465&6
2 900478&7
53 900443&4
6 900445&6
23 900467&8
16 900479&80
19 900487&8
12 900490&89
3 900491&2
26 900494&3
21 900495&6
9 900481&2
17 900483&4
27 900485&6
30 900497&8
51 900277&6
33 900275
27
22
35
19
9
7
21
28
10
39
20
25
11
8
38
24
23
30
36
29
1
5
14
16
18
17
6
2
3
33
32
31
37
12
1012
1010
1000
1001
1024
1016
1000
1010
1025
1010
1010
1030
1024
1025
1042
1020
742
1016
1025
984
850
862
633
938
1017
1000
1029
1031
1018
1010
1020
1010
1021
1036
1009
1247
1025
1003
955
1015
998
1021
1076
958
1017
1087
1081
961
1074
1024
726
1006
1042
995
836
859
629
904
1003
981
1006
1068
956
1018
1015
1003
1036
1098
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
MEK
(ug)
142
13
169
nd
117
170
340
304
174
315
732
671
177
284
772
553
113
295
nd
547
130
154
533
nd
27
nd
119
142
117
nd
97
103
nd
282
235
MIBK
(ug)
186
178
180
nd
163
175
223
203
244
284
539
490
294
350
655
411
1878
2459
nd
65
213
244
189
12
1386
nd
1616
1965
>1594
nd
138
147
nd
377
nd
TOLUENE
(ug)
78
85
74
nd
69
81
97
89
105
115
145
221
139
158
301
187
110
364
nd
208
92
106
83
nd
146
nd
81
95
80
nd
66
71
nd
43
nd
BUTYL
ACETATE
(ug)
24
25
22
nd
21
25
27
28
30
31
72
63
45
50
93
61
35
112
nd
66
27
29
23
nd
nd
nd
25
29
24
nd
20
22
nd
52
nd
ETHYL
BENZENE
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
XYLENES
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
20.6
nd
nd
nd
nd
27.8
nd
16.2
nd
nd
nd
nd
13.8
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
-------
TEST: ORGANICS #1
DATE: 06-16-92
METHOD: NIOSH 1300
ACUREX ACUREX
GRID LOC TUBE t SAMPLE t
P
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
P over
under
1A
2A
3A
IB
2B
38
TUBE BLN
EXHAUST
RECIRC
15
22
25
24
10
20
14
11
54
5
56
59
18
8
58
29
1
13
28
2
53
6
23
16
19
12
3
26
21
9
17
27
30
51
33
900433&4
900456&5
900457&8
900469&70
900435&6
900454&3
900459&60
900471&2
900437&8
900451&2
9004618,2
900473&4
900439&40
900450&49
900463&4
900475&6
900441&2
900447&8
900465&6
900478&7
900443&4
900445&6
900467&8
9004798.80
900487&8
9004908.89
9004918.2
9004948.3
9004958.6
900481&2
9004838.4
900485&6
9004978.8
9002778,6
900275
AVG FLOW
(L/MIN)
1.011
1.129
1.013
1.002
0.990
1.016
0.999
1.016
1.051
0.984
1.014
1.059
1.053
0.993
1.058
1.022
0.734
1.011
1.034
0.990
0.843
0.861
0.631
0.921
1.010
0.991
1.018
1.050
0.987
1.014
1.018
1.007
0.000
1.029
1.067
MEK
(mg/M3)
2.2
0.2
2.6
< MDL
1.9
2.7
5.4
4.8
2.6
5.1
11.5
10.1
2.7
4.5
11.6
8.6
2.4
4.6
< MDL
8.8
2.4
2.8
13.4
< MDL
0.4
< MDL
1.9
2.1
1.9
< MDL
1.5
1.6
< MDL
4.4
3.5
MIBK
(mg/M3)
2.9
2.5
2.8
< MDL
2.6
2.7
3.5
3.2
3.7
4.6
8.4
7.3
4.4
5.6
9.8
6.4
40.6
38.6
< MDL
1.0
4.0
4.5
4.8
0.2
21.8
< MDL
25.2
29.7
25.6
< MDL
2.2
2.3
< MDL
5.8
< MDL
PAGE 2 OF 2
D E INITIALS: BN 8. LJL
Q A INITIALS: LJL
BUTYL ETHYL
TOLUENE ACETATE BENZENE XYLENES
(mg/M3) (mg/M3) (mg/M3) (mg/M3)
1.2
1.2
1.2
< MDL
1.1
1.3
1.5
1.4
1.6
1.9
2.3
3.3
2.1
2.5
4.5
2.9
2.4
5.7
< MDL
3.3
1.7
2.0
2.1
< MDL
2.3
< MDL
1.3
1.4
1.3
< MDL
1.0
1.1
< MDL
0.7
< MDL
0.4
0.4
0.3
< MDL
0.3
0.4
0.4
0.4
0.5
0.5
1.1
0.9
0.7
0.8
1.4
0.9
0.8
1.8
< MDL
1.1
0.5
0.5
0.6
< MDL
< MDL
< MDL
0.4
0.4
0.4 i
< MDL
0.3
0.3
< MDL
0.8
< MDL
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
<
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
0.3
< MDL
< MDL
< MDL
< MDL
0.4
< MDL
0.3
< MDL
< MDL
< MDL
< MDL
0.2
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
-------
S
ORGANICS *1
DATE: 06-16-92
METHOD: NIOSH 1300
GRID CHART 1 - NEK
Painter Over
Painter Under
< MDL
INLET GRID A
1A
1.9
2A
2.1
3A
1.9
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
Q A 1NITIALS:UL
1 2
2.2 0.2
5 6
1.9 2.7
9 10
2.6 5.1
21 22
2.7 4.5
13 U
2.4 4.6
17 18
2.4 2.8
3 4
2.6 < MOL
7 8
5.4 . 4.8
11 12
11.5 10.1
23 24
11.6 8.6
15 16
< HDL 8.8
19 20
13.4 < MDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
2B
1.5
1.6
PAINT TYPE: LT GREEN PRIMER, GRAY TOP UNITS: ng/M3 GRID MDL: 0.0115 «g/SAMPLE EXHAUST DUCT: 4.4
OBJECT: AUXILIARY RAMP OSHA TWA:590 Mg/M3 PAINTER MDL: 0.0115 ng/SAMPLE RECIRC DUCT: 3.5
-------
ORGANICS #1
DATE: 06-16-92
METHOD: N10SH 1300
GRID CHART 2 - MIBK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN I LJL
0 A INITIALS:LJL
Painter Over
21.8
Painter Under
< NDL
INLET GRID A
1A
25.2
2A
29.7
3A
25.6
EXHAUST GRID
1234
2.9 2.5 2.8 < HDL
5 A 7 A
2.6 2.7 3.5 . 3.2
9 10 11 12
3.7 4.6 8.4 7.3
21 22 23 24
4.4 5.6 9.8 6.4
13 14 15 16
40.6 38.6 < MDL 1.0
17 18 19 20
4.0 4.5 4.8 0.2
Field Blank
< MDL
INLET GRID B
IB
< HDL
2B
2.2
38
2.3
PAINT TYPE: LT GREEN PRIMER. GRAY TOP UNITS: «g/M3 GRID MDL: 0.0095 •g/SAMPLE EXHAUST DUCT: 5.8
OBJECT: AUXILIARY RAMP OSHA TWA:205 «g/M3 PAINTER MDL: 0.0095 ng/SAMPLE RECIRC DUCT: < MDL
-------
ORGANICS *1
DATE: 06-16-92
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 6485
D E INITIALS:BN & UL
0 A INIT1ALS:LJL
Painter Over
2.3
Painter Under
< MDL
INLET GRID A
1A
1.3
2A
1.4
3A
1.3
EXHAUST GRID
1234
1.2 1.2 1.2 < MDL
5X7*
1.1 1.3 1.5 1.4
9 10 11 12
1.6 1.9 2.3 3.3
21 22 23 24
2.1 2.5 4.5 2.9
13 14 15 16
2.4 5.7 < MDL 3.3
17 18 19 20
1.7 2.0 2.1 < HDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
2B
1.0
3B
1.1
PAINT TYPE: LT GREEN PRIMER, GRAY TOP UNITS: mgflO GRID MDL: 0.0114 MO/SAMPLE EXHAUST DUCT: 0.7
OBJECT: AUXILIARY RAMP OSHA TWA:375 ng/M3 PAINTER MDL: 0.0114 ny/SAMPLE RECIRC DUCT: < MDL
-------
ORGANICS «1
DATE: 06-16-92
METHOD: NIOSH 1300
GRID CHART 4 - BUTYL ACETATE
Painter Over
< MOL
Painter Under
< HDL
INLET GRID A
1A
0.4
2A
0.4
3A
0.4
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN ft LJL
0 A INITIALS:LJL
1 2
0.4 0.4
5 6
0.3 0.4
9 10
0.5 0.5
21 22
0.7 0.8
13 14
0.8 1.8
17 18
0.5 0.5
3 4
0.3 < MOL
7 8
0.4 0.4
11 12
1.1 0.9
23 24
1.4 0.9
15 16
< NDL 1.1
•>
19 20
0.6 < NDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
0.3
3B
0.3
PAINT TYPE: LT GREEN PRIMER, GRAY TOP UNITS: mgflO GRID MDL: 0.0116 Mg/SAMPLE EXHAUST DUCT: 0.8
OBJECT: AUXILIARY RAMP OSHA TUA:710 «g/W PAINTER MDL: 0.0116 •g/SANPLE RECIRC DUCT: < MDL
-------
ORGAN ICS 411
DATE: 06-16-92
METHOD: NIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INIT1ALS:BN & LJL
0 A INITIALSrUL
Painter Over
< HDL
Painter Under
< NDL
INLET GRID A
1A
< HDL
2A
< NDL
3A
< MDL
1234
< NDL < MDL < MDL < NDL
5676
< MDL < NDL < MDL < NDL
9 10 11 12
< NDL < MDL < MDL < NDL
21 22 23 24
< NDL < MDL < NDL < NDL
13 14 15 16
< MDL < MDL < MDL < NDL
1
17 18 19 20
< NDL < HDL < NDL < MDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
28
< MDL
38
< HDL
PAINT TYPE: LT GREEN PRIMER. GRAY TOP UNITS: «g/M3 GRID MDL: 0.0117 •g/SANPLE EXHAUST DUCT: < MDL
OBJECT: AUXILIARY RAMP OSHA TWA:435 «g/tt PAINTER MDL: 0.0117 Mg/SAMPLE RECIRC DUCT: < NDL
-------
CJl
Ul
ORGANICS «1
DATE: 06-16-92
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
Painter Over
0.2
Painter Under
< HDL
INLET GRID A
1A
< HDL
2A
< HDL
3A
< HDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
0 A INITIALS:LJL
1 2 3
< MDL < HDL < MDL
567
< MDL < MDL < HDL
9 10 11
< HDL < HDL < HDL
21 22 23
0.3 < HDL < HDL
13 U 15
< HDL 0.4 < HDL
I
17 18 19
< HDL < HDL < HDL
4
< HDL
8
< HDL
12
< HDL
24
< HDL
16
0.3
20
< HDL
Field Blank
< HDL
INLET GRID B
IB
< HDL
2B
< HDL
3B
< HDL
PAINT TYPE: LT GREEN MlHER. GRAY TOP UNITS: ng/H3 GRID HDL: 0.0368 Mg/SAHPLE EXHAUST DUCT: < HDL
OBJECT: AUXILIARY RAHP OSHA TWA:435 mgflO PAINTER HDL: 0.0368 Mg/SAHPLE RECIRC DUCT: < HDL
-------
TEST: ORGANICS #2
DATE: 06-17-92 AM
METHOD: NIOSH 1300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER. GRAY TOPCOAT
OBJECT: AUXILIARY RAMP BOTTOMS
PAGE 1 OF 2
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE * SAMPLE 1 PUMP l(ml/min) (ml/min) (min)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
14 DUP
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
28
38
EXHAUST
RECIRC
113 900407&8
46 900419&20
116 900431&2
43 900509&10
111 900409&10
44 900421&2
35 900499&500
119 900511&2
52 900411&2
49 900423&4
40 900501&2
108 900513&4
42 900413&4
109 900425&6
110 900503&4
117 900515&6
31 900415&6
112 900427&8
120 900527&8
41 900505&6
114 900517&8
32 900417&8
38 900429&30
45 900508&7
115 900519&20
47 900374&5
118 900376&7 '
50 900401&2
106 900403&4
48 900405&6
34 900521&2
37 900523&4
107 900525&6
36 900266&7
39 900268&9
2
13
18
22
1
8
7
21
11
9
17
25
3
15
19
24
10
14
37
12
26
6
16
5
20
32
35
33
31
28
30
29
27
36
39
1033
1086
1054
1091
1102
1031
1094
1068
1056
1060
1054
1088
1073
1095
1039
1037
1050
632
1076
1084
847
1100
953
912
1081
1058
1056
1074
1053
1055
1070
990
1054
1061
1064
1018
1078
1059
1176
1143
1027
1096
1068
1067
1056
1045
1150
1045
1146
1034
1070 57??
1094
631
1067
1128
770
1121
947
918
1081
1040
1034
1050
1036
1028
1050
981
1148
1048
1067
59
59
0
0
59
59
57
0
59
59
57
56
59
59
0
0
59
59
59
57
56
59
0
57
0
58
58
59
59
59
59
59
59
49
48
MEK
(ug)
65
209
nd
71
nd
76
289
nd
204
285
401
339
81
389
nd
224
228
224
319
710
602
215
nd
3019
nd
702
15
82
nd
74
149
nd
nd
298
105
MIBK
(ug)
96
156
nd
nd
nd
102
252
nd
225
220
317
255
178
387
nd
246
370
384
726
485
244
310
nd
385
nd
419
nd
108
nd •
96
139
nd
nd
252
135
TOLUENE
(ug)
62
77
nd
nd
nd
61
122
nd
120
109
169
135 '
114
198
nd
127
201
208
399
302
129
165
nd
111
nd
229
nd
65
nd •
58
71
nd
nd
158
84
BUTYL
ACETATE
(ug)
18
25
nd
nd
nd
19
40
nd
37
34
59
46
32
65
nd
41
65
71
135
100
45
53
nd
86
nd
68
nd
20
nd
20
22
nd
nd
49
25
ETHYL
BENZENE
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
XYLENES
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
-------
TEST: ORGANICS #2 PAGE 2 OF 2
DATE: 06-17-92 AM D E INITIALS: BN & LJL
METHOD: NIOSH 1300 Q A INITIALS: LJL
BUTYL ETHYL
ACUREX ACUREX AV6 FLOW MEK MIBK TOLUENE ACETATE BENZENE XYLENES
GRID LOG TUBE t SAMPLE 1 (L/MIN) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
14 DUP
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
2B
3B
EXHAUST
RECIRC
113 900407&8
46 900419&20
116 900431&2
43 900509&10
111 900409&10
44 900421&2
35 900499&500
119 900511&2
52 900411&2
49 900423&4
40 900501&2
108 900513&4
42 900413&4
109 900425&6
110 900503&4
117 900515&6
31 900415&6
112 900427&8
120 900527&8
41 900505&6
114 900517&8
32 900417&8
38 900429&30
45 900508&7
115 900519&20
47 900374&5
118 900376&7
50 900401&2
106 900403&4
48 900405&6
34 900521&2
37 9005238.4
107 9005258,6
36 900266&7
39 900268&9
1.026
1.082
1.057
1.134
.123
.029
.095
.068
.062
.058
1.050
1.119
1.059
.121
.037
.054
.072
0.632
.072
.106
0.809
1.111
0.950
0.915
1.081
1.049
1.045
1.062
1.045
1.042
1.060
0.986
1.101
1.055
1.066
1.1 1.6 1.0 0.3 < MDL < MDL
3.3 2.4 1.2 0.4 < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
no sampleno sampleno sampleno sampleno sampleno sample
< MDL < MDL < MDL < MDL < MDL < MDL
1.3 1.7 1.0 0.3 < MDL < MDL
4.6 4.0 2.0 0.6 < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
3.3 3.6 1.9 0.6 MDL < MDL
4.6 3.5 1.7 0.5 MDL < MDL
6.7 5.3 2.8 1.0 MDL < MDL
5.4 4.1 2.2 0.7 MDL < MDl
1.3 2.8 1.8 0.5 MDL < MDL
5.9 5.9 3.0 1.0 MDL < MD.L
no sampleno sampleno sampleno sampleno sampleno sample
no sampleno sampleno sampleno sampleno sampleno sample
3.6 5.8 3.2 1.0 < MDL < MDL
6.0 10.3 5.6 1.9 < MDL < MDL
5.0 11.5 6.3 2.1 < MDL < MDL
11.3 7.7 4.8 1.6 < MDL < MDL
13.3 5.4 2.8 1.0 < MDL < MDL
3.3 4.7 2.5 0.8 < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
57.9 7.4 2.1 1.6 < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
11.5 6.9 3.8 1.1 < MDL < MDL
0.2 < MDL < MDL < MDL < MDL < MDL
1.3 1.7 1.0 0.3 < MDL < MDL
< MDL < MDL < MDL < MDL < MDL < MDL
1.2 1.6 0.9 0.3 < MDL < MDL
2.4 2.2 1.1 0.4 MDL < MDL
< MDL < MDL < MDL < MDL MDL < MDL
< MDL < MDL < MDL < MDL MDL < MDL
5.8 4.9 3.1 0.9 MDL < MDL
2.1 2.6 1.6 0.5 MOL < MDL
-------
cn
CO
TEST: ORGANICS #2
DATE: 06-17-92 AM
METHOD: NIOSH 1300
GRID CHART 1 - NEK
Painter, Over
11.5
Painter Under
0.2
INLET GRID A
1A
1.3
2A
< MDL
3A
1.2
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
0 A INITIALS:LJL
1
1.1
5
< MDL
9
3.3
21
1.3
13
3.6
17
3.3
234
3.3 no sample no sample
678
1.3 4.6 no sample
10 11 12
4.6 6.7 5.4
22 23 24
5.9 no sample no sample
14 15 16
6.0 11.3 13.3
5.0
18 19 20
no sample 57.9 no sample
INLET GRID B
IB
2.4
2B
< MDL
3B
< MDL
PAINT TYPE: LT GREEN PRIMER. GRAY TOP UNITS: mg/M3 GRID MDL: 0.0115 mg/SAMPLE EXHAUST DUCT: 5.8
OBJECT: AUXILIARY RAMP BOTTOMS OSHA TUA:590 mg/M3 PAINTER HDL: 0.0115 mg/SAMPLE RECIRC DUCT: 2.1
-------
TEST: ORGANICS #2
DATE: 06-17-92 AN
METHOD: NIOSH 1300
GRID CHART 2 - NIBK
Painter Over
6.9
Painter Under
< HDL
INLET GRID A
1A
1.7
2A
< HDL
3A
1.6
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN t LJL
0 A INITIALS:LJL
1
1.6
5
< HDL
9
3.6
21
2.8
13
5.8
17
4.7
234
2.4 no sample no sample
678
1.7 4.0 no sample
10 11 12
3.5 5.3 4.1
22 23 24
5.9 no sample no sample
14 15 16
10.3 7.7 5.4
11.5
18 19 20
no sample 7.4 no sample
INLET GRID B
1B
2.2
2B
< HDL
3B
< HDL
PAINT TYPE: LT GREEN PRIMER, GRAY TOP UNITS: «g/M3 GRID HDL: 0.0095 •g/SAMPLE EXHAUST DUCT: 4.9
OBJECT: AUXILIARY RAMP BOTTOMS OSHA TUA:205 «s/M3 PAINTER HDL: 0.0095 MB/SAMPLE RECIRC DUCT: 2.6
-------
TEST: ORGANICS *2
DATE: 06-17-92 AH
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E IHITIALS:BN & LJL
0 A INITIALS:LJL
Painter Over
3.8
Painter Under
< MDl
INLET GRID A
1A
1.0
2A
< MDL
3A
0.9
1234
1.0 1.2 no sample no sample
5678
< HDL 1.0 2.0 no sample
9 10 11 12
1.9 1.7 2.8 2.2
21 22 23 24
1.8 3.0 no sample no sample
13 14 15 16
3.2 5.6 4.8 2.8
6.3
17 18 19 20
2.5 no sample 2.1 no sample
INLET GRID B
IB
1.1
2B
< HDL
3B
< MDL
PAINT TYPE: LT GREEN PRIMER. GRAY TOP UNITS: MQ/M3 GRID HDL: 0.0114 m/SAKPLE EXHAUST DUCT: 3.1
OBJECT: AUXILIARY RAMP BOTTOMS OSHA TUA:375 Mg/N3 PAINTER MDL: 0.0114 mg/SAMPLE RECIRC DUCT: 1.6
-------
O)
TEST: ORGANICS 92
DATE: 06-17-92 AH
METHOD: NIOSH 1300
GRID CHART 4 - BUTYL ACETATE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
0 A INITIALS:LJL
Painter Over
1.1
Painter Under
< HDL
INLET GRID A
1A
0.3
2A
< HDL
3A
0.3
1234
0.3 0.4 no sample no sample
5678
< NDL 0.3 0.6 no sample
9 10 11 12
0.6 0.5 1.0 0.7
21 22 23 24
0.5 1.0 no sample no sanple
13 14 15 16
1.0 1.9 1.6 1.0
2.1
17 18 19 20
0.8 no sample 1.6 no sample
INLET GRID B
IB
0.4
2B
< NDL
3B
< NDL
PAINT TYPE: LT GREEN PRIHER, GRAY TOP UNITS: *g/N3 GRID NDL: 0.0116 og/SANPLE EXHAUST DUCT: 0.9
OBJECT: AUXILIARY RAHP BOTTOMS OSHA TWA:710 ng/N3 PAINTER NDL: 0.0116 ng/SANPLE RECIRC DUCT: 0.5
-------
TEST: ORGANICS *2
DATE: 06-17-92 AH
METHOD: MIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN 4 LJL
Q A INITIALS:LJL
Painter Over
< HDL
Painter Under
< HDL
INLET GRID A
1A
< HDL
2A
< HDL
3A
< HDL
1234
< HDL < HDL no sample no sample
5678
< HDL < HDL < HDL no sample
9 10 11 12
< HDL < HDL < HDL < HDL
21 22 23 24
< HDL < HDL no sample no sample
13 14 15 16
< HDL < HDL < HDL < HDL
< HDL
O
17 18 19 20
< HDL no sample < HDL no sample
INLET GRID B
1B
< HDL
2B
< HDL
3B
< HDL
PAINT TYPE: LT GREEN PRIMER. GRAY TOP UNITS: MQ/H3 GRID HDL: 0.0117 Mg/SAHPLE EXHAUST DUCT: < HDL
OBJECT: AUXILIARY RAMP BOTTOMS OSHA TWA:435 «g/M3 PAINTER HDL: 0.0117 Mg/SAHPLE RECIRC DUCT: < HDL
-------
TEST: ORGANICS #2
DATE: 06-17-92 AM
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
Painter Over
< MDL
Painter Under
< MDL
INLET GRID A
1A
2A
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
Q A INITIALS:LJL
1
< MDL
5
< MDL
9
< MDL
21
< HDL
13
< MDL
17
< MDL
234
< MDL no sample no sample
678
< MDL < MDL no sample
10 11 12
< MDL < MDL < MDL
22 23 24
< MDL no sample no sample
14 15 16
< MDL < MDL < MDL
< MDL
18 19 20
no sample < MDL no sample
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
PAINT TTPE: LT GREEN PRIMER, GRAY TOP UNITS: mg/M3 GRID MDL: 0.0368 mg/SAKPLE EXHAUST DUCT: < HDL
OBJECT: AUXILIARY RAMP BOTTOMS OSHA TUA:435 mg/M3 PAINTER MDL: 0.0368 ng/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGANICS #3
DATE: 06-17-92 PM
METHOD: NIOSH 1300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER
OBJECT: METAL & WOOD BOX
PAGE 1 OF 2
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE 1 SAMPLE 1 PUMP *(ml/min) (ml/min) (min)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
2B
3B
EXHAUST
RECIRC
ADDITIONAL
10
22
RECIRC
149 900813&4
135 9008258.6
132 900837&8
96 900849650
18 9008158,6
105 9008278.8
103 9008398,40
100 9008518,2
104 90081 78,8
91 9008298,30
136 900841&2
129 900853&4
131 900819&20
146 900831&2
134 900843&4
140 9008558,6
126 9008218,2
128 9008338,4
95 9008458,6
141 9008578,8
93 9008238,4
142 9008358,6
148 9008478,8
124 9008598,60
150 900386&7
101F 900388
94 900801&2
147 900803&4
143 900805&6
138 900807&8
139 900809&10
92 9008118,2
125 9002708,1
98 9002728,3
ORGANIC SPECIES
91 9008298,30
146 900831&2
98 9002728,3
21
1
25
20
18
14
26
24
19
10
8
22
2
17
5
32
12
6
15
9
16
11
13
29
31
33
38
28
37
17
30
35
36
39
10
17
39
1068
1143
1150
1081
1059
631
770
1070
1034
1094
1008
1091
1018
1096
918
1040
1128
1121
1146
1056
947
1067
1078
981
1036
1050
1067
1028
1067
1045
1050
1034
1048
1067
1094
1096
1067
1046
1126
1175
1073
1054
625
750
1160
1002
1072
1027
1274
1076
1125
907
1061
1084
1108
1181
1048
928
1112
1171
978
993
1045
1062
1012
1059
1024
1060
1023
1056
997
1072
1125
997
49
0
5
0
0
49
49
49
29
50
49
0
38
49
49
48
30
49
49
50
1
50
48
0
49
0
49
49
49
49
0
49
46
46
50
49
46
MEK
(ug)
412
nd
nd
nd
14
65
470
601
481
877
1178
nd
264
985
1038
1203
445
725
2632
1510
nd
852
5845
nd
133
nd
399
132
373
287
nd
323
1145
nd
2-METHOXY
ETHYL
ETHER
51
62
nd
MIBK
(ug)
339
nd
nd
nd
nd
196
314
467
667
1113
805
nd
270
1385
834
659
602
1094
71
81
nd
484
477
nd
236
nd
336
128
342
' 234
nd
275
680
606
ETHYL
ACETATE
nd
nd
706
TOLUENE
(ug)
nd
nd
nd
nd
nd
nd
17
nd
18
31
21
nd
nd
39
21
16
17
31
191
18
nd
13
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
16
14
BUTYL
ACETATE
(ug)
91
nd
nd
nd
nd
55
81
73
191
299
204
nd
73
374
208
152
167
293
269
168
nd
130
125
nd
61
nd
88
35
90
62
nd
73
161
136
ETHYL
BENZENE
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
XYLENES
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
20
14
nd
nd
54
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
-------
TEST: ORGAN I CS #3
DATE: 06-17-92 PM
METHOD: NIOSH 1300
ACUREX ACUREX
GRID LOC TUBE t SAMPLE t
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
2B
38
EXHAUST
RECIRC
149
135
132
96
18
105
103
100
104
91
135
129
131
146
134
140
126
128
95
141
93
142
148
124
150
101F
94
147
143
138
139
92
125
98
900813&4
900825&6
900837&8
900849&50
90081 5&6
900827&8
900839&40
900851&2
90081 78,8
900829&30
900841&2
9008538,4
9008198,20
900831&2
900843&4
900855&6
9008218.2
9008338,4
900845&6
9008578,8
9008238,4
9008358,6
9008478,8
9008598,60
9003868,7
900388
9008018,2
9008038,4
9008058,6
9008078,8
9008098,10
9008118,2
9002708,1
900272&3
PAGE 2 OF 2
D E INITIALS: BN 8, LJL
Q A INITIALS: LJL
BUTYL ETHYL
AVG FLOW MEK MIBK TOLUENE ACETATE BENZENE XYLENES
(L/MIN) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3)
1
1
1
1
i
.057
1345
1625
.077
0565
0.628
1
1
1
0
1
1
1
0
1
1
0
1
1
1
1
1
i
i
i
i
i
i
i
i
i
i
0.76
.115
.018
.083
0175
1825
.047
1105
9125
0505
.106
1145
1635
.052
9375
0895
1245
9795
0145
0475
0645
1.02
.063
0345
.055
0285
.052
.032
8.0
no sampleno
< MDL <
no sampleno
no sampleno
2.1
12.6
11.0
16.3
16.2
23.6
no sampleno
6.6
18.1
23.2
23.9
13.4
13.3
46.2
28.7
< MDL <
15.6
108.3
no sampleno
2.7
no sampleno
7.6
2.6
7.2
5.7
no sampleno
6.4
23.7
< MDL
2-METHOXY
6.5 < MDL
sampleno
sampl eno
1.8 < MDL < MDL
sampl eno
sampleno
sampl e
MDL < MDL < MDL < MDL < MDL
sampleno
sampl eno
sampleno
sampleno
6.4 < MDL
8.4
0.5
8.5 < MDL
22.6
20.6
16.1
sampleno
6.8 <
25.5
18.7
13.1
18.1
20.0
1.2
1.5
MDL <
8.9
8.8 <
sampl eno
4.7 <
sampl eno
6.4 <
2.6 <
6.6 <
4.6 <
sampleno
5.5 <
14.1
12.8
0.6
0.6
0.4
sampleno
MDL
0.7
0.5
0.3
0.5
0.6
3.4
0.3
MDL <
0.2
MDL
sampl eno
MDL
sampl eno
MDL
MDL
MDL
MDL
sampleno
MDL
0.3
0.3
sampleno
sampl eno
1.8
2.2
1.3
6.5
5.5
4.1
sampl eno
1.8
6.9
4.7
3.0
5.0
5.4
4.7
3.2
MDL
sampl eno
sampleno
MDL <
MDL <
MDL <
MDL <
MDL
MDL
sampleno
MDL <
MDL
MDL <
MDL <
MDL
MDL
MDL
MDL
MDL
2.4 < MDL
2.3 < MDL
sampl eno
sampl eno
1.2 < MDL <
sampl eno
1.7
0.7
1.7 »
1.2
sampl eno
1.4
3.3
2.9
sampleno
MDL
MDL
MDL
MDL
sampleno
MDL
MDL
MDL
sample
sample
MDL
MDL
MDL
MDL
0.4
0.3
sample
MDL
1.0
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
sample
MDL
sample
MDL
MDL
MDL
MDL
sample
MDL
MDL
MDL
ETHYL ETHYL
ADDITIONAL
10
22
RECIRC
ORGANIC SPECIES
91
146
98
9008298,30
9008318,2
9002728,3
1
i
i
.083
1105
.032
ETHER ACETATE
0.9 <
1.1 <
< MDL
MDL
MDL
14.9
-------
TEST: ORGANICS «3
DATE: 06-17-92 PN
METHOD: NIOSH 1300
GRID CHART 1 - MEK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & Ul
0 A INITIALS:LJL
Painter Over
2.7
Painter Under
no sample
INLET GRID A
1A
7.6
2A
2.6
3A
7-2
EXHAUST GRID
1234
8.0 no sample < HDL no sample
no sample 2.1 12.6 11.0
9 10 11 12
16.3 16.2 23.6 no sample
21 22 23 24
6.6 18.1 23.2 23.9
13 14 15 16
13.4 13.3 46.2 28.7
17 18 19 20
< NDL 15.6 108.3 no sample
INLET GRID B
1B
5.7
2B
no sample
3B
6.4
PAINT TYPE: LT GREEN PRIMER
OBJECT: METAL I MOOD BOX
UNITS: Mg/M3 GRID HDL: 0.0115 mg/SAMPLE EXHAUST DUCT: 23.7
OSHA TUA:590 mg/lO PAINTER NDL: 0.0115 mg/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGANICS *3
DATE: 06-17-92 PH
NETHOO: NIOSH 1300
GRID CHART 2 - NIBK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
0 A INITIALS:LJL
Painter Over
4.7
Painter Under
no sanple
INLET GRID A
1A
6.4
2A
2.6
3A
6.6
EXHAUST GRID
1234
6.5 no sanple < MOL no sample
5678
no sanple 6.4 8.4 . 8.5
9 10 11 12
22.6 20.6 16.1 no sanple
21 22 23 24
6.8 25.5 18.7 13.1
13 14 15 16
18.1 20.0 1.2 1.5
17 18 19 20
< MDL 8.9 8.8 no sanple
INLET GRID B
1B
4.6
2B
no sanple
3B
5.5
PAINT TYPE: LT GREEK PRIMER
OBJECT: METAL t UOOD BOX
UNITS: mgflO GRID HDL: 0.0095 MB/SAMPLE EXHAUST DUCT: 14.1
OSHA TUA:205 *g/M3 PAINTER HDL: 0.0095 iig/SAMPLE RECIRC DUCT: 12.8
-------
TEST: ORGANICS «
DATE: 06-17-92 PM
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN I LJL
0 A 1NITIALS.-LJL
O)
CO
Painter Over
< MDL
Painter Under
no sample
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
1234
< MDL no sample < MDL no sample
5678
no sample < MDL 0.5 < MDL
9 10 11 12
0.6 0.6 0.4 no sample
21 22 23 24
< MDL 0.7 0.5 0.3
13 14 15 16
0.5 0.6 3.4 0.3
17 IB 19 20
< MDL 0.2 < MDL no sample
INLET GRID B
IB
< MDL
28
no sample
3B
< MDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: METAL I WOOD BOX
UNITS: Mg/M3 GRID MDL: 0.0114 mg/SAMPLE EXHAUST DUCT: 0.3
OSHA TWA:375 Mg/M3 PAINTER MDL: 0.0114 «g/SAMPLE RECIRC DUCT: 0.3
-------
TEST: ORGANICS «
DATE: 06-17-92 PM
METHOD: NIOSH 1300
GRID CHART 4 - BUTYL ACETATE
Painter Over
1.2
Painter Under
no sample
INLET GRID A
1A
1.7
2A
0.7
1.7
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
Q A INITIALS:LJL
1 2 3
1.8 no sample < HDL
5 6 7
no sample 1.8 2.2
9 10 11
6.5 5.5 4.1
21 22 23
1.8 6.9 4.7
13 14 15
5.0 5.4 4.7
17 18 19
< HDL 2.4 2.3
4
no sample
8
1.3
12
no sample
24
3.0
16
3.2
20
no Maple
PAINT TTPE: LT GREEN PRIMER
OBJECT: METAL t WOOD BOX
INLET GRID B
IB
1.2
2B
no sample
3B
1.4
UNITS: *a/M3 GRID MOL: 0.0116 Mg/SAMPLE EXHAUST DUCT: 3.3
OSHA TUA:710 ng/W PAINTER HDL: 0.0116 ng/SANPLE RECIRC DUCT: 2.9
-------
TEST: ORGANICS «
OKIE: 06-17-92 PN
METHOD: MIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITtALS:BN I LJL
Q A INITIALS:LJL
Painter Over
< MDL
Painter Under
no sample
INLET GRID A
1A
< MDL
2A
< MDL
3A
< HDL
EXHAUST GRID
1234
< MDL no sample < MDL no sample
5678
no sample < MDL < MDL < MDL
9 10 11 12
< MDL < MDL < MDL no sample
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL < MDL < MDL < MDL
•
17 18 19 20
< MDL < MDL < MDL no sample
INLET GRID B
IB
< MDL
28
no sample
3B
< MDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: METAL I WOOD BOX
UNITS: M9/M3 GRID MDL: 0.0117 ng/SAMPLE EXHAUST DUCT: < MDL
OSHA TUA:435 ng/M3 PAINTER MDL: 0.0117 ng/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGAN ICS *3
DATE: 06-17-92 PM
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
0 E IN1T1ALS:BN & LJL
0 A INITIALS:LJL
Painter Over
< MDL
Painter Under
no sample
INLET GRID A
1A
2A
< NDL
3A
< NDL
1234
< NDL no sample < MDL no sample
5678
no sample < HDL < NDL < NDL
9 10 11 12
< NDL 0.4 0.3 no sample
21 22 23 24
< HDL 1.0 < HDL < NDL
4
13 14 15 16
< HDL < MDL < HDL < NDL
17 18 19 20
< NDL < NDL < NDL no sample
INLET GRID 8
IB
< MDL
28
no sample
3B
< NDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: METAL t WOOD BOX
UNITS: mg/M3
OSHA TUA:435 mg/M3
GRID MDL: 0.0368 ng/SAMPLE EXHAUST DUCT: < NDL
PAINTER HDL: 0.0368 Mg/SANPLE RECIRC DUCT: < NDL
-------
TEST: ORGANICS #4 TRAVIS AFB PAINT: LT GREEN PRIMER
DATE: 06/18/92 PAINT BOOTH TESTS OBJECT: LADDERS
METHOD: NIOSH 1300 ACUREX PROJECT 8485
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME MEK MIBK
GRID LOC TUBE t SAMPLE * PUMP l(ml/min) (ml/min) (min) (ug) (ug)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
13 DUP
14
15
16
17
18
18 DUP
19
20
P over
P under
1A
2A
3A
IB
2B
3B
EXHAUST
RECIRC
174 900867&88
122 900869&70
162 900873&4
178 900875&6
171 900877&8
133 900879&80
173 900881&2
121 900883&4
163 900885&6
172 900887&8
164 900889&90
166 900891&2
165 900907&8
160 900909&10
153 900911&2
151 900913&4
167 900893&81
127 900921&2
170 900894&72
203 900895&6
152 900897&8
130 900899&900
155 900901&2
97 900923&4
169 900903&4
154 900905&6
176 900378&9
175F 900380
177 900861&2
161 900863&4
179 900865&6
168 900915&6
157 900917&B
158 900919&20
156 900274&8
159 900279&80
1
24
20
18
5
32
34
19
6
13
8
35
15
17
31
37
2
12
10
9
7
14
25
11
26
33
21
30
3
38
27
16
29
28
36
39
1055
1071
1089
1060
890
1053
1001
1023
1009
1060
1023
1041
1089
1053
1036
1042
1060
1050
1077
1089
1066
800
1022
1033
876
1020
1044
1054
1057
1051
1002
935
978
1025
1009
1030
1080
1128
1082
1060
878
1043
1002
1033
1027
994
1016
1029
1077
1046
1029
1046
1082
1043
1037
1078
1014
530
1053
1046
874
1027
1040
1065
1056
1046
1019
915
968
1033
1049
1028
0
1
1
0
30
29
0
0
29
28
29
29
30
29
29
29
22
29
29
30
30
29
29
30
29
0
28
0
29
29
29
25
28
29
31
30
nd
nd
nd
nd
31
39
nd
nd
32
60
107
68
40
71
117
75
56
50
128
200
106
94
420
455
421
nd
nd
nd
48
45
50
nd
42
35
199
76
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
18
nd
nd
13
24
nd
nd
nd
25
56
20
nd
111
nd
132
nd
nd
nd
nd
nd
nd
nd
nd
nd
59
nd
TOLUENE
(ug)
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd'
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
^d
nd
nd
nd
PAGE 1 OF 2
BUTYL ETHYL
ACETATE BENZENE XYLENES
(ug) (ug) (ug)
nd
nd
nd
nd
13
nd
nd
nd
22
nd
nd
30
31
nd
nd
nd
34
32
nd
nd
nd
nd
nd
16
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
14
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
nd
-------
CO
TEST: ORGANICS #4 PAGE 2 OF 2
DATE: 06/18/92 0 E INITIALS: BN & LJL
METHOD: NIOSH 1300 Q A INITIALS: LJL
BUTYL ETHYL
ACUREX ACUREX AVG FLOW MEK MIBK TOLUENE ACETATE BENZENE XYLENES
GRID LOG TUBE t SAMPLE 1 (L/MIN) (Mg/M3) (ug/M3) (ug/M3) (ug/M3) (ug/M3) (ug/M3)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
13 DUP
14
15
16
17
18
18 DUP
19
20
P over
P under
1A
2A
3A
IB
2B
3B
EXHAUST
RECIRC
174 900867&88
122 900869&70
162 900873&4
178 900875&6
171 900877&8
133 900879&80
173 900881&2
121 900883&4
163 900885&6
172 900887&8
164 900889&90
166 900891&2
165 900907&8
160 900909&10
153 900911&2
151 900913&4
167 900893&81
127 900921&2
170 900894&72
203 900895&6
152 900897&8
130 900899&900
155 900901&2
97 9009238.4
169 900903&4
154 900905&6
176 900378&9
175F 900380
177 900861&2
161 900863&4
179 900865&6
168 900915&6
157 900917&8
158 900919&20
156 900274&8
159 900279&80
1.068
1.100
1.086
,1.060
0.884
1.048
1.002
1.028
1.018
1.027
1.020
1.035
1.083
1.050
1.033
1.044
1.071
1.047
1.057
1.084
1.040
0.665
1.038
1.040
0.875
.024
.042
.060
.057
.049
.011
0.925
0.973
.029
.029
.029
no sampleno sampleno sampleno sampleno sampleno sample
< MDL < MDL < MDL < MDL < MDL < HDL
< MDL < MDL < MDL < MDL < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
1.2 < MDL < MDL 0.5 < MDL < MDL
1.3 < MDL < MDL < MDL < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
no sampleno sampleno sampleno sampleno sampleno sample
1.1 < MDL < MDL 0.7 < MDL < MDL
2.1 < MDL < MDL < MDL < MDL < MDL
3.6 0.6 < MDL < MDL < MDL < MDL
2.3 < MDL < MDL 1.0 < MDL < MDL
1.2 < MDL < MDL 1.0 < MDL f- MDL
2.3 0.4 < MDL < MDL < MDL < MDL
3.9 0.8 < MDL < MDL < MDL < MDL
2.5 < MDL < MDL < MDL < MDL < MDL
2.4 < MOL < MDL 1.4 < MDL < MDL
1.6 < MDL < MDL 1.1 < MDL < MDL
4.2 0.8 < MDL < MDL < MDL < MDL
6.2 1.7 < MDL < MDL < MDL < MDL
3.4 0.6 < MDL < MDL < MDL < MDL
4.9 < MDL < MDL < MDL < MDL < MDL
14.0 3.7 < MDL < MDL < MDL < MDL
14.6 < MDL < MDL 0.5 < MDL < MDL
16.6 5.2 < MDL < MDL < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
< MDL < MDL < MDL < MDL < MDL < MDL
no sampleno sampleno sampleno sampleno sampleno sample
.6 < MDL < MDL < MDL < MDL < MDL
.5 < MDL < MDL < MDL < MDL < MDL
.7 < MDL < MDL < MDL < MDL < MDL
< MDL < MDL < MDL < MDL < MDL o < MDL
.5 < MDL < MDL < MDL < MDL < MDL
.2 < MDL < MDL < MDL < MDL < MDL
6.2 1.8 < MDL 0.4 < MDL < MDL
2.5 < MDL < MDL < MDL < MDL < MDL
-------
TEST: ORGANICS «4
DATE: 06/18/92
METHOD: NIOSH 1300
GRID CHART 1 - NEK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALSrBN & LJL
0 A INITIALS:LJL
Painter Over
< NDL
Painter Under
no sample
INLET GRID A
1A
1.6
2A
1.5
3A
1.7
1234
no sample < NDL < NDL no sample
5A T A
1.2 1.3 no sample no sample
9 10 11 12
1.1 2.1 3.6 2.3
21 22 23 24
1.2 2.3 3.9 2.5
13 14 15 16
2.4 4.2 6.2 3.4
1.6
17 18 19 20
4.9 14.0 16.6 no sample
14.6
INLET GRID B
IB
< NDL
2B
1.5
38
1.2
PAINT TYPE: LT GREEN PRIMER
OBJECT: LADDERS
UNITS: wg/W GRID NDL: 0.0115 ng/SANPLE EXHAUST DUCT: 6.2
OSHA TWA:590 «g/N3 PAINTER NDL: 0.0115 ng/SANPLE RECIRC DUCT: 2.5
-------
TEST: ORGANICS *4
DATE: 06/18/92
METHOD: NIOSH 1300
GRID CHART 2 - MIBK
Painter Over
< HDL
Painter Under
no sample
IMLET GRID A
1A
< MDL
2A
< NDL
3A
< NDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN ft LJL
0 A INITIALS:LJL
1 2
no sample < NDL
5 6
< NDL < NDL
9 10
< NDL < HDL
21 22
< HDL 0.4
13 14
< HDL 0.8
< NDL
17 18
< HDL 3.7
< NDL
3 4
< NDL no sample
7 8
no sample no sample
11 12
0.6 < HDL
23 24
0.8 < HDL
IS 16
1.7 0.6
1
19 20
5.2 no sample
PAINT TYPE: LT GREEN PRIHER
OBJECT: LADDERS
INLET GRID B
IB
< NDL
28
< HDL
3B
< HDL
UNITS: mgflO GRID HDL: 0.0095 mg/SAHPLE EXHAUST DUCT: 1.8
OSHA TWA:205 Mg/N3 PAINTER HDL: 0.0095 mg/SAHPLE RECIRC DUCT: < HDL
-------
TEST: ORGANICS *4
DATE: 06/18/92
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN I LJL
0 A INITIALS:LJL
Painter Over
< HDL
Painter Under
no sample
INLET GRID A
1A
< HDL
2A
< HDL
3A
< HDL
EXHAUST GRID
1234
no sample < NDL < HDL no sample
5 A 7 A
< NDL < NDL no sample . no sample
9 10 11 12
< HDL < HDL < HDL < HDL
21 22 23 24
< HDL < HDL < HDL < HDL
13 14 15 16
< HDL < HDL < HDL < HDL
< HDL •
17 IB 19 20
< HDL < HDL < HDL no sample
< HDL
INLET GRID B
1B
< HDL
2B
< HDL
3B
< HDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: LADDERS
UNITS: ng/N3 GRID HDL: 0.0114 ing/SANPLE EXHAUST DUCT: < HDL
OSHA TUA:375 ng/N3 PAINTER HDL: 0.0114 ng/SANPLE RECIRC DUCT: < HDL
-------
TEST: ORGANICS *4
DATE: 06/18/92
METHOD: NIOSH 1300
GRID CHART 4 - BUTYL ACETATE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
0 A INITIALS:LJL
Painter Over
< HDL
Painter Under
no sample
INLET GRID A
1A
< NDL
2A
< NDL
3A
< NDL
EXHAUST GRID
1234
no sample < NDL < NDL no sanple
5 A 7 A
0.5 < NDL no sanple . no sanple
9 10 11 12
0.7 < NDL < NDL 1.0
21 22 23 24
1.0 < NDL < NDL < NDL
13 14 15 16
1.4 < NDL < NDL < NDL
1.1
17 18 19 20
< HDL < NDL < NDL no sample
0.5
INLET GRID B
1B
< NDL
2B
< NDL
3B
< NDL
PAINT TYPE: LT GREEN PRINER
OBJECT: LADDERS
UNITS: ng/N3 GRID NDL: 0.0116 ng/SANPLE EXHAUST DUCT: 0.4
OSHA TWA:710 MB/N3 PAINTER NDL: 0.0116 ag/SANPLE RECIRC DUCT: < NDL
-------
TEST: ORGAN ICS *4
DATE: 06/18/92
METHOD: NIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
0 E INITIALS:BN & LJL
0 A INITIALS:UL
Painter Over
< HDL
Painter Under
no sanple
INLET GRID A
1A
< MDL
2A
< HDL
3A
< HDL
EXHAUST GRID
1234
no sample < MDL < MDL no sample
5 A 7 A
< MDL < HDL no sanple no sample
9 10 11 12
< HDL < HDL < MDL < MDL
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL < MDL < MDL < MDL
< MDL
17 18 19 20
< MDL < HDL < HDL no sanple
< HDL
INLET GRID B
1B
< MDL
2B
< HDL
SB
< MDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: LADDERS
UNITS: «g/M3 GRID MDL: 0.0117 •g/SAMPLE EXHAUST DUCT: < HDL
OSHA TUA:435 Bg/W PAINTER MDL: 0.0117 ng/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGANICS *4
DATE: 06/18/92
METHOD: MIOSH 1300
GRID CHART 6 - XYLENES
Painter Over
< HDL
Painter Under
no sample
INLET GRID A
1A
< HDL
2A
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
0 E INITIALS:BN t LJL
Q A INITIALS:LJL
1 2
no sacnple < MDL
5 6
< MDL < MDL
9 10
< MDL < MDL
21 22
< MDL < MDL
13 14
< MDL < MDL
< MDL
17 18
< MDL < MDL
< MDL
3 4
< MDL no sample
7 8
no sample no sample
11 12
< MDL < MDL
23 24
< MDL < MDL
15 16
< MDL < MDL
19 20
< MDL no sample
PAINT TYPE: LT GREEN PRIMER
OBJECT: LADDERS
INLET GRID B
IB
< MDL
2B
< MDL
38
< MDL
UNITS: H9/M3 GRID MDL: 0.0368 Mg/SAMPLE EXHAUST DUCT: < MDL
OSHA TUA:435 «g/M3 PAINTER MDL: 0.0368 HO/SAMPLE RECIRC DUCT: < MDL
-------
TEST: OR6ANICS #5
DATE: 06-23-92 PM
METHOD: NIOSH 1300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: WHITE TOPCOAT
OBJECT: COMFORT PALLET
PAGE 1 OF 2
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE 1 SAMPLE 1 PUMP #(ml/min) (ml/min) (min)
1
2
3
4
5
6
7
8
9
9 DUP
10
11
12
12 DUP
21
22
23
24
13
14
15
15 DUP
16
17
18
18 DUP
19
20
P over
P OVER 2
1A
2A
3A
IB
2B
3B
3B DUP
F BLANK
EXHAUST
RECIRC
211 900943&4
198 900945&6
190 900947&8
238 900949&50
186 900951&2
196 900953&4
183 900955&6
215 900957&8
236 900959&60
60x 900927
192 900961&2
217 900963&4
219 900965&6
230 900994&5
237 900967&8
216 900969&70
226 900971&2
212 900973&4
235 900975&6
225 900977&8
181 900979&80
184 900992&3
240 900981&2
233 900983&4
214 900985&6
200x 900991
223 900987&8
188 900989&90
228 900390&1
102F 900392
222 900931&2
194 900933&7
239 900934&8
213 9009358.6
182 9009398,40
224 900941 8,2
145F 900925
55F 900926
185 900291&0
187 900288&9
40
18
42
35
33
8
10
21
41
2
12
25
16
43
15
13
9
29
11
17
7
6
5
1
24
14
20
34
30
19
28
27
3
31
22
32
23
38
39
1063
1028
1050
1040
1017
1017
1051
1011
1077
1050
1096
1047
1040
1073
1081
1023
1071
1026
1060
1029
1022
1031
1095
1040
1031
1009
1056
1076
1023
1042
1028
1070
1078
1075
1057
1040
848
TEST
1011
1053
1045
1029
1044
1031
1009
1000
1043
1004
1056
1050
1061
994
988
1055
1042
974
1052
1025
1041
1017
1000
1043
1106
1041
1035
1017
1035
1073
1011
1025
1041
1044
1073
1068
1043
1032
862
TIME ->
994
1025
0
0
58
58
0
59
61
58
60
45
59
58
58
0
60
57
60
0
60
58
60
58
59
0
59
59
58
0
0
59
59
59
59
59
51
59
59
55
68
69
MEK
(ug)
ND
ND
76
79
ND
103
111
131
75
104
149
223
183
ND
86
190
444
ND
82
208
551
583
302
ND
387
294
949
ND
ND
524
62
69
82
164
65
63
109
ND
223
448
MIBK
(ug)
ND
ND
415
347
ND
554
609
562
330
461
1073
755
761
ND
377
1176
1226
ND
454
1022
1227
1370
842
ND
605
544
921
ND
ND
3824
255
352
336
333
363
224
426
ND
437
711
TOLUENE
(ug)
ND
ND
73
66
ND
104
102
97
65
85
192
133
133
ND
74
210
213
ND
81
189
208
238
152
ND
111
101
166
ND
ND
1113
51
73
65
65
65
46
80
ND
80
115
BUTYL
ACETATE
(ug)
ND
ND
111
91
ND
148
158
141
77
129
297
193
193
13
103
318
348
ND
121
284
344
371
224
ND
166
137
249
ND
ND
1053
ND
94
88
85
99
65
117
ND
117
178
ETHYL
BENZENE XYLENES
(ug) (ug)
ND
NO
ND
ND
ND
ND
ND
ND
14
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
21
ND
ND
ND
ND
ND
ND
15
ND
67
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
14
ND
18
12
12
ND
ND
22
21
ND
ND
18
20
36
14
ND
ND
ND
16
ND
ND
106
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
-------
00
TEST: ORGANICS #5
DATE: 06-23-92 PM
METHOD: NIOSH 1300
ACUREX ACUREX
GRID LOG
P
F
1
2
3
4
5
6
7
8
9
9 DUP
10
11
12
12 DUP
21
22
23
24
13
14
15
15 DUP
16
17
18
18 DUP
19
20
P over
OVER 2
1A
2A
3A
IB
28
38
3B DUP
BLANK
EXHAUST
RECIRC
TUBE *
211
198
190
238
186
196
183
215
236
60x
192
217
219
230
237
216
226
212
235
225
181
184
240
233
214
200x
223
188
228
102F
222
194
239
213
182
224
145F
55F
185
187
SAMPLE t
900943&4
900945&6
900947&8
900949&50
900951&2
900953&4
900955&6
900957&8
900959&60
900927
900961&2
900963&4
900965&6
9009948,5
900967&8
900969&70
900971&2
900973&4
900975&6
900977&8
900979&80
900992&3
900981&2
900983&4
900985&6
900991
900987&8
900989&90
900390&1
900392
900931&2
900933&7
900934&8
900935&6
900939&40
900941&2
900925
900926
900291&0
900288&9
AVG
PAGE 2 OF 2
D E INITIALS: BN & LJL
Q A INITIALS: LJL
BUTYL ETHYL
FLOW MEK MIBK TOLUENE ACETATE BENZENE XYLENES
(L/MIN)
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
0
1
1
1
1
1
1
1
1
1
1
.054
.029
.047
.036
.013
.009
.047
.008
.067
.050
.079
.021
.014
.064
.062
.999
.062
.026
.051
.023
.011
.037
.101
.041
.033
.013
.046
.075
.017
.034
.035
.057
.076
.072
.050
.036
.855
.000
.003
.039
(mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3)
no sampleno
no sampleno
1.3
1.3
no sampleno
1.7
1.7
2.2
1.2
2.2
2.3
3.8
3.1
no sampleno
1.4
3.3
7.0
no sampleno
1.3
3.5
9.1
9.7
4.7
no sampleno
6.3
4.9
15.6
no sampleno
no sampleno
8.6
1.0
1.1
1.3
2.6
1.2
1.0
2.2
< MDL <
3.3
6.2
sampl eno
sampl eno
6.8
5.8
sampl eno
9.3
9.5
9.6
5.2
9.8
16.9
12.8
12.9
sampl eno
5.9
20.7
19.2
sampl eno
7.2
17.2
20.2
22.8
13.0
sampleno
9.9
9.1
15.2
sampleno
sampleno
62.7
4.2
5.6
5.3
5.3
6.8
3.7
8.4
MDL <
6.4
9.9
sampl eno
sampl eno
1.2
1.1
sampleno
1.7
1.6
1.7
1.0
1.8
3.0
2.2
2.3
sampl eno
1.2
3.7
3.3
sampleno
1.3
3.2
3.4
4.0
2.3
sampl eno
1.8
1.7
2.7
sampleno
sampl eno
18.3
0.8 <
1.2
1.0
1.0
1.2
0.8
1.6
MDL <
1.2
1.6
sampl eno
sampleno
1.8 <
1.5 <
sampl eno
2.5 <
2.5 <
2.4 <
1.2
2.7 <
4.7 <
3.3 <
3.3 <
sampl eno
1.6 <
5.6 <
5.5 <
sampl eno
1.9 <
4.8 <
5.7
6.2 <
3.4 <
sampl eno
2.7 <
2.3 <
4.1 <
sampleno
sampleno
17.3
MDL <
.5 <
.4 <
.3 <
.8
.1
2.3
MDL
1.7
2.5
sampl eno
sampl eno
MDL <
MDL <
sampl eno
MDL <
MDL <
MDL <
0.2
MDL <
MDL
MDL
MDL
sampl eno
MDL <
MDL
MDL
sampl eno
MDL <
MDL
0.3
MDL
MDL
sampleno
MDL <
MDL <
MDL
sampleno
sampleno
1.1
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
sample
sample
MDL
MDL
sample
MDL
MDL
MDL
0.2
MDL
0.3
0.2
0.2
sampl e
MDL
0.4
0.3
sample
MDL
0.3
0.3
0.6
0.2
sample
MDL
MDL
0.3
sample
sample
1.7
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
-------
TEST: ORGANICS «
DATE: 06-23-92 PN
METHOD: NIOSH 1300
GRID CHART 1 - MEK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & UL
0 A INITIALS:UL
CO
10
Painter Over
no sanple
Painter Under
8.6
INLET GRID A
1A
1.0
2A
1.1
3A
1.3
1234
no sanple no sanple 1.3 1.3
5 A 7 ft
no sanple 1.7 1.7 2.2
9 10 11 12
1.2 2.3 3.8 . 3.1
2.2 no sanple
21 22 23 24
1.4 3.3 7.0 no sample
13 14 15 16
1.3 3.5 9.1 4.7
9.7
17 18 19 20
no saaple 6.3 15.6 no sanple
4.9
Field Blank
< MOL
INLET GRID B
IB
2.6
2B
1.2
3B
1.0
2.2
PAINT TYPE: WHITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: mg/N3
OSHA TWA:590 «g/M3
GRID MDL: 0.0115 «g/SAMPLE EXHAUST DUCT: 3.3
PAINTER M)L: 0.0115 ng/SANPLE RECIRC DUCT: 6.2
-------
TEST: ORGANICS *5
DATE: 06-23-92 PM
METHOD: NIOSH 1300
GRID CHART 2 - HIBK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
Q A INITIALS:!..)!.
Painter Over
no sample
Painter Under
62.7
INLET GRID A
1A
4.2
2A
5.6
3A
5.3
EXHAUST GRID
1234
no sample no sample 6.8 5.8
5678
no sanple 9.3 9.5 9.6
9 10 • 11 12
5.2 16.9 12.8 12.9
9.8 no sample
21 22 23 24
5.9 20.7 19.2 no sample
13 14 15 16
7.2 17.2 20.2 13.0
22.8
a
17 18 19 20
no sanple 9.9 15.2 no sanple
9.1
Field Blank
< HDL
INLET GRID B
IB
5.3
2B
6.8
3B
3.7
8.4
PAINT TYPE: UNITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: ng/M3 GRID MDL: 0.0095 ng/SAMPLE EXHAUST DUCT: 6.4
OSHA TWA:205 ng/W PAINTER HDL: 0.0095 ng/SANPLE RECIRC DUCT: 9.9
-------
TEST: ORGANICS f5
DATE: 06-23-92 PN
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
Q A 1NITIALS:LJL
Painter Over
no sample
Painter Under
18.3
INLET GRID A
1A
0.8
2A
1.2
3A
1.0
EXHAUST GRID
1234
no sample no sample 1.2 1.1
5678
no sample 1.7 1.6 1.7
9 10 11 12
1.0 3.0 2.2 2.3
1.8 no sample
21 22 23 24
1.2 3.7 3.3 no sample
13 14 15 16
1.3 3.2 3.4 2.3
4.0
17 18 19 20
no sample 1.8 2.7 no sample
1.7
Field Blank
< HDL
INLET GRID B
IB
1.0
28
1.2
3B
0.8
1.6
PAINT TYPE: UNITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: ng/M3 GRID MDL: 0.0114 ng/SAHPLE EXHAUST DUCT: 1.2
OSHA TWA:375 Mg/N3 PAINTER MDL: 0.0114 mg/SAMPLE RECIRC DUCT: 1.6
-------
TEST: ORGAN1CS f5
DATE: 06-23-92 PN
METHOD: MIOSH 1300
GRID CHART 4 - BUTYL ACETATE
Painter Over
no sample
Painter Under
17.3
INLET GRID A
1A
< HDL
2A
1.5
3A
1.4
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
0 E INITIALS:BN & LJL
0 A INITIALS:LJL
1 2 3
no sample no sample 1.8
567
no sample 2.5 2.5
9 10 11
1.2 4.7 3.3
2.7
21 22 23
1.6 5.6 5.5
13 14 15
1.9 4.8 5.7
6.2
17 18 19
no sample 2.7 4.1
2.3
4
1.5
8
2.4
12
3.3
no sample
24
no sample
16
3.4
20
no sample
Field Blank
< MDL
INLET GRID B
IB
1.3
2B
1.8
36
1.1
2.3
PAINT TYPE: UNITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: •g/N3
OSHA TUA:710 «g/M3
GRID MDL: 0.0116 •g/SANPLE EXHAUST DUCT: 1.7
PAINTER MDL: 0.0116 MB/SAMPLE RECIRC DUCT: 2.5
-------
TEST: ORGANICS *5
DATE: 06-23-92 PM
METHOD: NIOSH 1300
GRID CHART 5 - ETHYL BENZENE
Painter Over
no sample
Painter Under
1.1
INLET GRID A
1A
< M>L
2A
< HDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN t LJL
Q A INITIALS:LJL
1 2 3
no sample no sample < MDL
567
no sample < NOL < MDL
9 10 11
0.2 < MDL < MDL
< MDL
21 22 23
< HDL < MDL < MDL
13 U 15
< MDL < MDL 0.3
• 0.3
17 18 19
no sample < MDL < MDL
< MDL
4
< MDL
8
< MDL
12
< MDL
no sample
24
no sample
16
< MDL
20
no sample
PAINT TYPE: UNITE TOPCOAT
OBJECT: COMFORT PALLET
Field Blank
< MDL
INLET GRID B
1B
< MDL
28
< HDL
38
< MDL
< HDL
UNITS: rna/M GRID MDL: 0.0117 mg/SAMPLE EXHAUST DUCT: < MDL
OSHA TUA:435 mg/M3 PAINTER MDL: 0.0117 Mg/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGANICS «5
DATE: 06-23-92 PM
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
0 E INITIALS:BN t LJL
0 A INITIALS:LJL
23
Painter Over
no saiple
Painter Under
1.7
INLET GRID A
1A
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
no sanple no sanple < MDL < MDL
5678
no sample < MDL < MDL . < MDL
9 10 11 12
0.2 0.3 0.2 0.2
< MDL no sample
21 22 23 24
< MDL 0.4 0.3 no sanple
13 14 15 16
< MDL 0.3 0.3 0.2
• 0.6
17 IB 19 20
no sanple < MDL 0.3 no sanple
< MDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
2B
< MDL
38
< MDL
< HDL
PAINT TYPE: WHITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: •o/MS GRID MDL: 0.0368 ng/SAMPLE EXHAUST DUCT: < MDL
OSHA TUA:435 «g/M3 PAINTER MDL: 0.0368 •g/SAMPLE RECIRC DUCT: < MDL
-------
TEST: OR6ANICS #6
DATE: 06-30-92 PM
METHOD: NIOSH 1300
TRAVIS AFB PAINT:
PAINT BOOTH TESTS OBJECT:
ACUREX PROJECT 8485
GUNSHIP GRAY TOPCOAT
C141 ENGINE
PAGE 1 OF 2
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE t SAMPLE t PUMP #(ml/min) (ml/min) (tnin)
1
2
3
3 DUP
4
5
6
7
8
9
10
11
11 DUP
12
21
22
22 DUP
23
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
2A DUP
3A
IB
2B
3B
F BLANK
EXHAUST
RECIRC
86 900999&1000
63 901001&2
249 901003&4
241 901005&6
77 901007&8
257 901009&10
71 901011&2
268 901013&4
65 901015&6
85 901017&8
259 901019&20
73 9010218,2
75 901027&8
68 901023&4
242 901043&4
66 901045&6
84 901047&8
62 901049&50
260 901051&2
69 901025&6
80 901029&30
251 901031&2
81 901033&4
72 901035&6
267 901037&8
263 901039&40
76 901041&2
61 900297&394
89F 900393
266F 900395
67 900397&8
70 900399&400
90 900796&7
266B 900798
78 900800&996
246 900997&8
89B 900296
245 900292&3
265 900294&5
35
5
29
20
50
11
17
28
24
6
34
15
8
14
13
43
12
1
25
16
47
33
32
30
40
18
45
46
52
55
31
21
51
49
54
19
37
38
1057
1056
1053
1081
1049
1054
1053
1076
1053
1096
1052
1053
1081
1085
1076
1045
1050
1056
1053
1077
1041
1045
1063
1039
1040
1028
1072
1112
1051
1036
1036
1075
1049
1049
1058
1045
1056
1027
1047
1015
912
1075
1046
1085
1015
1078
1070
1068
1037
1080
1018
775
1043
1042
1074
553
1068
1140
1041
1032
1079
1036
1039
1015
974
1112
928
1019
1022
1067
1047
1055
960
1018
1022
1012
64
65
46
64
64
65
64
64
65
64
64
65
65
47
62
64
64
48
17
64
64
64
65
64
0
64
47
0
64
63
63
0
63
64
42
63
63
57
57
MEK
(ug)
49
49
54
76
69
53
73
75
83
47
60
181
137
88
48
54
60
60
NO
61
86
314
125
49
ND
1160
352
ND
ND
45
35
ND
39
28
25
32
ND
42
39
MIBK TOLUENE
(ug) (ug)
850
909
564
999
679
1048
1107
1165
1047
948
1227
2410
2185
623
945
1143
1135
779
281
941
1437
2655
1001
763
ND
1277
604
ND
106
716
582
ND
584
644
349
581
ND
1112
1061
47
54
53
58
38
56
54
48
34
46
58
75
68
57
44
28
40
51
37
60
63
71
46
60
75
49
55
41
371
66
32
34
43
65
42
45
120
50
50
BUTYL
ACETATE
(ug)
245
265
163
285
197
309
318
303
294
279
361
688
635
174
282
324
311
242
86
276
410
740
266
227
ND
327
160
ND
31
208
178
ND
173
200
146
160
ND
323
307
ETHYL
BENZENE XYLENES
(ug) (ug)
ND
ND
ND
13
ND
ND
ND
15
13
ND
13
33
30
ND
ND
14
13
ND
ND
12
19
35
13
ND
ND
14
ND
ND
ND
ND
ND
ND
ND
ND
11
15
ND
11
NO
58
63
41
73
50
76
72
70
67
67
85
161
149
43
69
77
71
64
ND
70
102
163
58
59
ND
53
32
ND
ND
50
45
DN
44
54
28
39
ND
78
74
-------
TEST: ORGANICS #6 PAGE 2 OF 2
DATE: 06-30-92 PM D E INITIALS: BN & LJL
METHOD: NIOSH 1300 Q A INITIALS: LJL
BUTYL ETHYL
ACUREX ACUREX AVG FLOW MEK MIBK TOLUENE ACETATE BENZENE XYLENES
GRID LOG TUBE 1 SAMPLE * (L/MIN) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3) (mg/M3)
1
2
3
3 DUP
4
5
6
7
8
9
10
11
11 DUP
12
21
22
22 DUP
23
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
2A DUP
3A
IB
2B
3B
F BLANK
EXHAUST
RECIRC
86 900999&1000
63 901001&2
249 901003&4
241 901005&6
77 9010078.8
257 901009&10
71 901011&2
268 901013&4
65 901015&6
85 9010178,8
259 901019&20
73 9010218,2
75 9010278,8
68 901023&4
242 901043&4
66 901045&6
84 901047&8
62 9010498.50
260 901051&2
69 9010258.6
80 9010298.30
251 901031&2
81 901033&4
72 901035&6
267 901037&8
263 901039&40
76 901041&2
61 900297&394
89F 900393
266F 900395
67 9003978,8
70 900399&400
90 900796&7
266B 900798
78 9008008,996
246 900997&8
89B 900296
245 900292&3
265 9002948,5
1.052
1.036
0.983
1.078
1.048
1.070
1.034
1.077
1.062
1.082
1.045
1.067
1.050
0.930
1.060
1.044
1.062
0.805
1.061
1.109
1.041
1.039
1.071
1.038
1.040
1.022
1.023
1.112
0.990
1.028
1.029
1.071
1.048
1.052
1.009
1.032
1.000
1.039
1.020
0.7 12.6 0.7 3.6 < MDL 0.9
0.7 13.5 0.8 3.9 < MDL 0.9
1.2 12.5 1.2 3.6 < MDL 0.9
1.1 14.5 0.8 4.1 0.2 1.1
1.0 10.1 0.6 2.9 < MDL 0.7
0.8 15.1 0.8 4.4 < MDL 1.1
1.1 16.7 0.8 4.8 < MDL 1.1
1.1 16.9 0.7 4.4 0.2 1.0
1.2 15.2 0.5 4.3 0.2 1.0
0.7 13.7 0.7 4.0 < MDL 1.0
0.9 18.4 0.9 5.4 0.2 1.3
2.6 34.8 1.1 9.9 0.5 2.3
2.0 32.0 1.0 9.3 0.4 2.2
2.0 14.3 1.3 4.0 < MDL 1.0
0.7 14.4 0.7 4.3 < MDL 1.1
0.8 17.1 0.4 4.9 0.2 1.2
0.9 16.7 0.6 4.6 0.2 1.0
1.6 20.2 1.3 6.3 < MDL 1.7
< MDL 15.6 2.1 4.8 < MDL < MDL
0.9 13.3 0.8 3.9 0.2 1.0
1.3 21.6 0.9 6.2 0.3 1.5
4.7 39.9 1.1 11.1 0.5 2.5
1.8 14.4 0.7 3.8 0.2 0.8
0.7 11.5 0.9 3.4 < MDL 0.9
no sampleno sampleno sampleno sampleno sampleno sample
17.7 19.5 0.7 5.0 0.2 0.8
7.3 12.6 1.1 3.3 < MDL 0.7
no sampleno sampleno sampleno sampleno sampleno sample
< MDL 1.7 5.9 0.5 < MDL < MDL
0.7 11.1 1.0 3.2 < MDL 0.8
0.5 9.0 0.5 2.7 < MDL 0.7
no sampleno sampleno sampleno sampleno sampleno sample
0.6 8.8 0.7 2.6 < MDL 0.7
0.4 9.6 1.0 3.0 < MDL 0.8
0.6 8.2 1.0 3.4 0.3 0.7
0.5 8.9 0.7 2.5 0.2 0.6
< MDL < MDL 1.9 < MDL < MDL < MDL
0.7 18.8 0.8 5.5 0.2 1.3
0.7 18.3 0.9 5.3 < MDL 1.3
-------
TEST: ORGANICS «6
DATE: 06-30-92 PM
METHOD: MIOSH 1300
GRID CHART 1 - MEK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN I LJL
0 A INITIALSiLJL
Painter Over
no sample
Painter Under
< MDL
INLET GRID A
1A
0.7
2A
0.5
no caopte
SA
0.6
1
1234
0.7 0.7 1.2 1.0
1.1
5 A 7 ft
0.8 1.1 1.1 1.2
9 10 11 12
0.7 0.9 2.6 2.0
2.0
21 22 23 24
0.7 0.8 1.6 < HDL
0.9
13 14 15 16
0.9 1.3 4.7 1.8
17 16 19 20
0.7 no saaple 17.7 7.3
Field Blank
< MDL
INLET GRID B
IB
0.4
2B
0.6
38
0.5
PAINT TYPE: OUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
UNITS: ng/M3 GRID MDL: 0.0115 ng/SAMPLE EXHAUST DUCT: 0.7
OSHA TWA:590 «g/M3 PAINTER MDL: 0.0115 ng/SAMPLE RECIRC DUCT: 0.7
-------
CD
TEST: ORGANICS «6
DATE: 06-30-92 PN
METHOD: NIOSH 1300
GRID CHART 2 - NIBK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
0 A INITIALS:LJL
Painter Over
no sample
Painter Under
1.7
INLET GRID A
1A
11.1
2A
9.0
no saaple
3A
8.8
;
1234
12.6 13.5 12.5 10.1
14.5
5676
15.1 16.7 16.9 15.2
9 10 11 12
13.7 18.4 34.8 14.3
32.0
21 22 23 24
14.4 17.1 20.2 15.6
16.7
13 14 15 16
13.3 21.6 39.9 14.4
17 18 19 20
11.5 no saof>le 19.5 12.6
Field Blank
< MDL
INLET GRID B
IB
9.6
2B
8.2
38
8.9
PAINT TYPE: GUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
UNITS: mgflO GRID MDL: 0.0095 MO/SAMPLE EXHAUST DUCT: 18.8
OSHA TWA: 205 ng/M3 PAINTER MDL: 0.0095 Mg/SAMPLE RECIRC DUCT: 18.3
-------
(D
10
TEST: ORGANICS #6
DATE: 06-30-92 PH
METHOD: N10SH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
0 A INIT1ALS:LJL
Painter Over
no sample
Painter Under
5.9
INLET GRID A
1A
1.0
2A
0.5
no sample
3A
0.7
;
EXHAUST GRID
1234
0.7 0.8 1.2 0.6
0.8
5 A 7 A
0.8 0.8 0.7 0.5
9 10 11 12
0.7 0.9 1.1 1.3
1.0
21 22 23 24
0.7 0.4 1.3 2.1
0.6
13 14 15 16
0.8 0.9 1.1 0.7
ft
17 18 19 20
0.9 no sanple 0.7 1.1
Field Blank
1.9
INLET GRID 8
IB
1.0
2B
1.0
3B
0.7
PAINT TYPE: GUNSHIP GRAY TOPCOAT UNITS: mgflQ GRID HDL: 0.0114 Mg/SAHPLE EXHAUST DUCT: 0.8
OBJECT: C141 ENGINE OSHA TWA:375 «9/W PAINTER MDL: 0.0114 MB/SAMPLE RECIRC DUCT: 0.9
-------
TEST: ORGANICS #6
DATE: 06-30-92 PN
METHOD: NIOSH 1300
GRID CHART 4 - BUTYL ACETATE
Painter Over |
no swple I
Painter Under I
0.5
INLET GRID A
1A
3.2
2A
2.7
no sample
3A
2.6
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN I LJL
Q A INITIALS:LJL
1
3.6
5
4.4
9
4.0
21
4.3
13
3.9
17
3.4
234
3.9 3.6 2.9
4.1
678
4.8 4.4 4.3
10 11 12
5.4 9.9 4.0
9.3
22 23 24
4.9 6.3 4.8
4.6
14 15 16
6.2 11.1 3.8
»
18 19 20
no sample 5.0 3.3
PAINT TYPE: GUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
Fietd Blank
< NDL
INLET GRID B
IB
3.0
2B
3.4
2.5
UNITS: mgflO GRID MDL: 0.0116 MB/SAMPLE EXHAUST DUCT: 5.5
OSHA TUA:710 •0/N3 PAINTER MDL: 0.0116 MO/SAMPLE RECIRC DUCT: 5.3
-------
TEST: ORGANICS «6
DATE: 06-30-92 PM
METHOD: NIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN & LJL
Q A INITIALS:LJL
Painter Over
no sample
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
no ample
3A
< MDL
;
EXHAUST GRID
1234
< MDL < MDL < MDL < MDL
0.2
< MDL < MDL 0.2 0.2
9 10 11 12
< MDL 0.2 0.5 < MDL
0.4
21 22 23 24
< MDL 0.2 < MDL < MDL
0.2
13 14 15 16
0.2 0.3 0.5 0.2
I
17 18 19 20
< MDL no sanple 0.2 < MDL
Field Blank
< MOL
INLET GRID B
IB
< MDL
2B
0.3
3B
0.2
PAINT TTPE: GUNSHIP GRAY TOPCOAT UNITS: ng/M3 GRID MDL: 0.0117 •g/SAMPLE EXHAUST DUCT: 0.2
OBJECT: C141 ENGINE OSHA TWA:435 Mg/N3 PAINTER MDL: 0.0117 ng/SAMPLE RECIRC DUCT: < MDL
-------
TEST: ORGANICS «6
DATE: 06-30-92 PH
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
Painter Over |
no sample I
Painter Under I
< NDL I
INLET GRID A
1A
0.8
2A
0.7
no sample
3A
0.7
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN & LJL
Q A IMITIALSrLJL
1
0.9
5
1.1
9
1.0
21
1.1
13
1.0
17
0.9
234
0.9 0.9 0.7
1.1
678
1.1 1.0 1.0
10 11 12
1.3 2.3 1.0
2.2
22 23 24
1.2 1.7 < NDL
1.0
14 15 16
1.5 2.5 0.8
18 19 20
no sample 0.8 0.7
Field Blank
< MDL
INLET GRID B
1B
0.8
2B
0.7
3B
0.6
PAINT TYPE: GUNSHIP GRAY TOPCOAT UNITS: MQ/N3 GRID NDL: 0.0368 ng/SAHPLE EXHAUST DUCT: 1.3
OBJECT: C141 ENGINE OSHA TUA:435 ng/K3 PAINTER NDL: 0.0368 mg/SAMPLE RECIRC DUCT: 1.3
-------
TEST: SINGLE PASS ORGAN1CS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: GUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
PAGE 1 OF 2
\
ACUREX ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC TUBE 1 SAMPLE I PUMP #(m1/m1n) (ml/rain) (min)
1
2
3
3 DUP
4
5
6
7
8
9
10
11
11 DUP
12
21
22
22 DUP
23
24
13
14
15
15 DUP
16
17
18
19
20
P over
P under
1A
2A
3A
IB
28
3B
F BLANK
EXHAUST
SPLIT
321 9003898,96
322 900529&30
297 900799&928
248 901319&8
301 900929&30
299 901053&4
303 901055&6
296 901057&8
290 901059&60
305 901286&7
291 901288&9
292 901290&1
293 901320&1
312 901292&3
244 901310&1
294 901312&3
302 901322&3
64 901314&5
320 901316&7
315 901294&5
306 901296&7
300 901298&9
307 901324&5
308 901300&1
289 9013028,3
323 901304&5
298 901306&7
309 901308&9
313 9003278.8
253F 900329
311 9003498,62
281F 900363
280F 900364
295 9003658,82
88F 900383
318 9003848,5
304 9002878,308
310 9003098,26
34
33
54
28
18
42
11
13
47
30
31
17
35
50
29
19
7
10
51
24
20
53
12
43
45
15
5
55
49
52
36
39
32
16
6
1
37
38
1056
1051
1048
1035
1034
1022
997
1005
997
1043
1052
991
1068
1029
986
1005
1034
1014
1001
1032
1007
1029
1029
1063
1006
1025
1004
1053
1007
1020
1012
1006
1033
958
1036
997
1029
1020
1022
1036
1031
1009
1018
1004
1010
1021
985
1051
1021
971
1051
1007
972
970
1048
957
1010
1020
997
1023
1042
1034
1032
1052
963
1032
989
970
1025
1044
1043
1001
1020
964
1014
993
67
1
67
67
68
67
68
66
68
0
67
67
67
68
1
67
68
68
68
67
67
67
68
68
67
68
68
67
67
67
67
67
67
67
67
68
63
60
MEK
(ug)
ND
NO
17
17
22
13
19
26
24
ND
23
47
46
37
ND
19
19
39
31
ND
20
63
58
27
ND
36
258
65
28
ND
ND
ND
ND
ND
ND
ND
20
18
MIBK
(ug)
70
ND
159
' 181
135
148
297
379
231
ND
312
896
1053
320
ND
291
301
958
333
96
370
841
986
231
82
'231
353
176
215
ND
ND
ND
ND
ND
ND
ND
222
221
TOLUENE
(ug)
ND
ND
17
ND
15
ND
ND
NO
ND '
13
ND .
24
26
ND
ND
16
ND
26
ND
27
16
ND
13
ND
33
ND
ND
ND
27
35
NO
ND
ND
ND
ND
ND
13
ND
BUTYL
ACETATE
(ug)
36
ND
34
55
44
51
104
125
79
ND
99
321
372
108
ND
93
103
363
110
NO
112
267
323
69
ND
65
87
55
129
30
ND
ND
ND
ND
ND
ND
74
74
ETHYL
BENZENE XYLENES
(ug) (ug)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
13
15
ND
ND
ND
ND
15
NO
ND
ND
11
14
ND
ND
ND
ND
ND
15
15
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
29
ND
ND
ND
87
94
ND
ND
ND
ND
99
ND
ND
26
67
190
ND
ND
ND
ND
ND
17
ND
ND
ND
ND
ND
ND
ND
ND
ND
-------
TEST: SINGLE PASS ORGANICS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
ACUREX ACUREX
GRID LOG TUBE 1 SAMPLE «
1
2
3
3 DUP
4
5
6
7
8
9
10
11
11 DUP
12
21
22
22 DUP
23
24
13
14
15
15 DUP
16
17
18
19
20
P over
P under
F
1A
2A
3A
IB
2B
3B
BLANK
EXHAUST
SPLIT
321
322
297
248
301
299
303
296
290
305
291
292
293
312
244
294
302
64
320
315
306
300
307
308
289
323
298
309
313
253F
311
281F
280F
295
88F
318
304
310
900389&96
900529&30
900799&928
901319&8
9009298.30
9010538.4
901055&6
901057&8
901059&60
9012868.7
9012888.9
901290&1
901320&1
901292&3
901310S1
9013128.3
901322&3
901314&5
901316&7
901294&5
901296&7
9012988.9
901324&5
901300&1
9013028.3
901304&5
901306&7
901308&9
900327&8
900329
900349&62
900363
900364
900365&82
900383
900384&5
9002878.308
900309&26
PAGE 2 OF 2
D E INITIALS: BN 8. LJL
Q A INITIALS: LJL
BUTYL ETHYL
AVG FLOW MEK MI8K TOLUENE ACETATE BENZENE XYLENES
(L/MIN) (mg/M3) (mg/M3) (mg/M3) (ntg/M3) (mg/M3) (mg/M3)
1.039
1.0435
1.0395
1.022
1.026
1.013
1.0035
1.013
0.991
1.047
1.0365
0.981
1.0595
1.018
0.979
0.9875
1.041
0.9855
1.0055
1.026
1.002
1.026
1.0355
1.0485
1.019
1.0385
0.9835
1.0425
0.998
0.995
1.0185
1.025
1.038
0.9795
1.028
0.9805
0
1.0215
1.0065
< MDL
< MDL
0.2
0.2
0.3
0.2
0.3
0.4
0.4
no sampleno
0.3
0.7
0.6
0.5
< MDL
0.3
0.3
0.6
0.5
< MDL
0.3
0.9
0.8
0.4
< MDL
0.5
3.9
0.9
0.4
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
no sampleno
0.3
0.3.
1.0
< MDL
2.3
2.6
1.9
2.2
4.4
5.7
3.4
sampleno
4.5
13.6
14.8
4.6
< MDL
4.4
4.3
14.3
4.9
1.4
5.5
12.2
14.0
3.2
1.2
3.3
5.3
2.5
3.2
MDL
MDL
MDL
MDL
MDL
MDL
MDL
sampl eno
3.4
3.7
< MDL
0.5
< MDL < MDL
0.2
< MDL '
0.2
< MDL
< MDL
< MDL
< MDL
sampleno
< MDL
0.4
0.4
< MDL
< MDL <
0.2
< MDL
0.4
< MDL
0.4 <
0.2
< MDL
0.2
< MDL
0.5 . <
MDL
MDL
MDL
0.4
0.5
MDL
MDL
MDL
MDL
MDL
MDL <
sampleno
0.2
< MDL
0.5
0.8
0.6
0.8
1.5
1.9
1.2
< MDL
< MOL
< MDL
< MDL
MDL
MDL
MDL <
MDL
MDL <
sampleno sampleno
1.4
4.9
5.2
1.6
MDL
1.4
1.5
5.4
1.6
MDL
1.7
3.9
4.6
1.0
MDL
0.9
1.3
0.8
1.9
0.5
MDL
MDL
MDL
MDL
MDL
MDL
sampleno
1.1
1.2
< MDL <
0.2
0.2
< MDL <
< MDL <
< MDL <
< MDL <
0.2
< MDL <
< MDL <
< MDL
0.2
0.2
< MDL <
< MDL <
< MDL <
< MDL <
< MDL <
0.2
0.2
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
MDL
0.4
MDL
sample
MDL
1.3
1.3
MDL
MDL
MDL
MDL
1.5
MDL
MDL
0.4
1.0
2.7
MDL
MDL
MDL
MDL
MDL
0.3
MDL
MDL
MDL
MDL
MDL
MDL
MDL
sampleno sample
MDL <
MDL <
MDL
MDL
-------
TEST: S.P. ORGANICS
DATE: 07-01-92 AMI
METHOD: MIOSH 1300
GRID CHART 1 - NEK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN t LJL
0 A INITIALS:UL
Painter Over
0.4
Painter Under
< NDL
INLET GRID A
1A
< HDL
2A
< HDL
3A
< NDL
1234
< NDL < MDL 0.2 0.3
0.2
5 A 7 ft
0.2 0.3 0.4 0.4
9 10 11 12
no swple 0.3 0.7 0.5
0.6
21 22 23 24
< NDL 0.3 0.6 0.5
0.3
13 14 15 16
< NDL 0.3 0.9 0.4
0.8
17 18 19 20
< NDL 0.5 3.9 0.9
Field Blank
no sample
INLET GRID B
IB
< NDL
2B
< NDL
3B
< NDL
PAINT TYPEiGUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
UNITS: «g/N3 GRID NDL: 0.0115 Mg/SANPLE EXHAUST DUCT: 0.3
OSHA TUA:S90 ng/IG PAINTER NDL: 0.0115 ng/SANPLE SINGLE PASS DUCT: 0.3
-------
TEST: S.P. ORGANICS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
GRID CHART 2 - NIBK
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INIT1AIS:BN I LJL
Q A INITIALS:LJL
Painter Over
3.2
Painter Under
< NDL
INLET GRID A
1A
< NDL
2A
< HDL
3A
< NDL
EXHAUST GRID
1234
1.0 < MDL 2.3 1.9
2.6
5 A 7 It
2.2 4.4 5.7 3.4
9 10 11 12
no sanple . 4.5 13.6 4.6
14.8
21 22 23 24
< MDL 4.4 14.3 4.9
4.3
13 14 15 16
1.4 5.5 12.2 3.2
14.0
17 18 19 20
1.2 3.3 5.3 2.5
Field Blank
no sample
INLET GRID B
1B
< MDL
28
< NDL
38
< NDL
PAINT TYPE:GUNSHIP GRAY TOPCOAT UNITS: wg/KJ GRID MDL: 0.0095 ng/SANPLE EXHAUST DUCT: 3.4
OBJECT: C141 ENGINE OSHA TWA:205 mgflO PAINTER MDL: 0.0095 •g/SAMPLE SINGLE PASS DUCT: 3.7
-------
8
TEST: S.P. ORGANICS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
GRID CHART 3 - TOLUENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS:BN I LJL
Q A 1NITIALS:LJL
Painter Over
0.4
Painter Under
0.5
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
< MDL < MDL 0.2 0.2
< MDL
5678
< MDL < MDL < MDL < MDL
9 10 11 12
no sample < MDL 0.4 < MDL
0.4
21 22 23 24
< MDL 0.2 0.4 < MDL
< MDL
13 14 15 16
0.4 0.2 < MDL < MDL
0.2
17 18 19 20
0.5 < MDL < MDL < MDL
Field Blank
no sample
INLET GRID B
1B
< MDL
2B
< MDL
3B
< MDL
PAINT TYPE:QUNSHIP GRAY TOPCOAT UNITS: «9/M3 GRID MDL: 0.0114 Mg/SAMPLE EXHAUST DUCT: 0.2
OBJECT: C141 ENGINE OSHA TUA:375 «g/M3 PAINTER MDL: 0.0114 Mg/SAMPLE SINGLE PASS DUCT: < MDL
-------
TEST: S.P. ORGANICS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
GRID CHART I • BUTYL ACETATE
Painter Over
1.9
Painter Under
0.5
INLET GRID A
1A
< HDL
2A
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN t LJL
0 A INITIALS:LJL
1 2
0.5 < MDL
5 6
0.8 1.5
9 10
no sample 1.4
21 22
< MDL 1.4
1.5
13 14
< MDL 1.7
17 18
< MDL 0.9
3 4
0.5 0.6
0.8
7 8
1.9 1.2
11 12
4.9 1.6
5.2
23 24
5.4 1.6
15 16
3.9 1.0
4.6
19 20
1.3 0.8
Field Blank
no sanple
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
PAINT TTPE:GUNSHIP OUT TOPCOAT UNITS: Mg/M3 GRID HDL: 0.0116 MB/SAMPLE EXHAUST DUCT: 1.1
OBJECT: C141 ENGINE OSHA TUA:710 mg/IO PAINTER MDL: 0.0116 MO/SAMPLE SINGLE PASS DUCT: 1.2
-------
TEST: S.P. ORGANICS
DATE: 07-01-92 AM1
METHOD: NIOSH 1300
GRID CHART 5 - ETHYL BENZENE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS:BN t LJL
0 A INITIALS:UL
Painter Over
0.2
Painter Under
0.2
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
1234
< MDL < MDL < MDL < MDL
< MDL
5 6 7 8
< MDL < MDL < MDL < MDL
9 10 11 12
no sample < NDL 0.2 < MDL
0.2
21 22 23 24
< MDL < HDL 0.2 < MDL
< MDL
13 H 15 16
< MDL < MDL 0.2 < NDL
0.2
O
17 18 19 20
< NDL < MDL < MDL < MDL
Field Blank
no sample
INLET GRID B
1B
< MDL
28
< NDL
3B
< NDL
PAINT TYPE:GUNSHIP GRAY TOPCOAT
OBJECT: CU1 ENGINE
UNITS: B9/M3 GRID MDL: 0.0117 ag/SAMPLE EXHAUST DUCT: < MDL
OSHA TUA:435 wg/M3 PAINTER MDL: 0.0117 ^/SAMPLE SINGLE PASS DUCT: < NDL
-------
8
TEST: S.P. ORGANICS
DATE: 07-01-92 AMI
METHOD: NIOSH 1300
GRID CHART 6 - XYLENES
Painter Over
0.3
Painter Under
< MDL
INLET GRID A
1A
< NDL
2A
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E 1NITIALS:BN I LJL
0 A INITIALS:LJL
1 2
< MDL < MDL
$ 6
< MDL < MDL
9 10
no aaqpte < NDL
21 22
< MDL < MDL
< MDL
13 U
< MDL 0.4
17 18
< MDL < NDL
3 4
< HDL < NDL
< HDL
7 8
0.4 < NDL
11 12
1.3 < HDL
1.3
23 24
1.5 < MDL
15 16
1.0 < MDL
2.7
O
19 20
< MDL < NDL
PAINT TTPE:GUNSHIP GRAY TOPCOAT
OBJECT: C141 ENGINE
Field Blank
no sample
INLET GRID B
IB
< HDL
2B
< NDL
3B
< HDL
UNITS: «g/N3 GRID MDL: 0.0368 Mg/SANPLE EXHAUST DUCT: < HDL
OSHA TWA: 435 mQ/M PAINTER NDL: 0.0368 ng/SANPLE SINGLE PASS DUCT: < HDL
-------
TEST: PARTICULATE 01
DATE: 06-19-92 AM
METHOD: NIOSH 500
ACUREX
GRID LOG SAMPLE 0 FILTER * PUMP
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: WHITE TOPCOAT
OBJECT: LADDERS
D E INITIALS: BN t LJL
Q A INITIALS: LJL
(RAW DATA, BALANCE ACCURACY 0.0001)
PRE-CAL POST-CAL RUN TIME PRE «1 PRE 92 POST 01 POST 02 AVG FLOW PRE AVG POST AVG PART UT PARTICULATE
(nt/min) (ml/nin) (min) (g) (g) (g) (g) (L/MIN) (g) (g) (g) (mg/M3)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
24
13
13 DUP
14
15
16
17
18
18 DUP
19
20
P over
? under
1A
2A
3A
18
2B
3B
EXHAUST
RECIRC
900077
900078
900079
900080
900081
900082
900083
900084
900085
900086
900087
900088
900089
900090
900091
900092
900093
900094
900095
900096
900097
900098
900099
900100
900101
900102
900137
900136
900071
900072
900073
900074
900075
900076
33
162
88
24
16
94
92
71
67
133
134
151
84
31
116
28
17
2
22
5
6
40
102
21
69
85
203
152
160
185
9
53
157
82
29
4
24
20
35
2
19
7
32
30
26
12
34
22
18
9
31
23
6
5
8
33
36
1
25
11
28
21
14
15
10
3
13
27
3024
3072
3024
3085
3045
3042
3075
3066
3057
3079
3069
3027
3015
3003
3054
3018
3091
3075
3036
3057
3082
3066
3048
3048
3003
3048
3069
3042
3054
3027
3006
3045
3054
3024
2988
3017
3113
3066
3000
3126
3012
3048
2962
3003
2962
3088
2991
3135
3045
3027
3045
3129
3036
3036
3054
3039
3060
3018
3060
3122
3006
3000
3107
3018
2983
3024
3048
3012
42
42
42
41
42
32
41
42
42
42
42
42
41
37
41
44
41
42
42
42
42
42
42
43
42
42
41
41
42
42
42
41
41
41
0.0132
0.0128
0.0116
0.0118
0.0125
0.0130
0.0126
0.0121
0.0119
0.0128
0.0132
0.0132
0.0128
0.0133
0.0125
0.0125
0.0125
0.0126
0.0136
0.0125
0.0115
0.0132
0.0132
0.0123
0.0115
0.0125
0.0120
0.0128
0.0122
0.0118
0.0119
0.0117
0.0132
0.0124
0.0132
0.0127
0.0116
0.0118
0.0125
0.0130
0.0126
0.0121
0.0120
0.0128
0.0131
0.0132
0.0128
0.0133
0.0125
0.0124
0.0125
0.0125
0.0135
0.0124
0.0115
0.0131
0.0133
0.0123
0.0116
0.0124
0.0120
0.0128
0»0122
0.0118
0.0120
0.0117
0.0133
0.0124
0.0132
0.0127
0.0116
0.0118
0.0126
0.0132
0.0126
0.0120
0.0125
0.0129
0.0131
0.0132
0.0135
0.0135
0.0125
0.0124
0.0136
0.0135
0.0140
0.0126
0.0115
0.0143
0.0142
0.0126
0.0120
0.0125
0.0171
0.0128
0.0122
0.0118
0.0119
0.0117
0.0132
0.0123
0.0132
0.0127
0.0116
0.0118
0.0126
0.0132
0.0125
0.0121
0.0125
0.0130
0.0131
0.0132
0.0134
0.0135
0.0126
0.0125
0.0136
0.0136
0.0140
0.0125
0.0115
0.0143
0.0142
0.0126
0.0119
0.0126
0.0170
0.0128
0.0122
0.0119
0.0120
0.0118
0.0132
0.0124
3.006
3.045
3.069
3.076
3.023
3.084
3.044
3.057
3.010
3.041
3.016
3.058
3.003
.069
.050
.023
.068
.102
.036
.047
3.068
3.053
3.054
3.033
3.032
3.085
3.038
3.021
3.081
3.023
2.995
3.035
3.051
3.018
0
0
0.0132
0.0128
0.0116
0.0118
0.0125
0.0130
0.0126
0.0121
0.0119
0.0128
0.0131
0.0132
0.0128
0.0133
0.0125
0.0125
0.0125
0.0125
0.0135
0.0124
0.0115
0.0132
0.0133
0.0123
0.0115
0.0124
0.0120
0.0128
0.0122
0.0118
0.0120
0.0117
0.0132
0.0124
0
0
0.0132
0.0127
0.0116
0.0118
0.0126
0.0132
0.0125
0.0120
0.0125
0.0130
0.0131
0.0132
0.0134
0.0135
0.0125
0.0124
0.0136
0.0135
0.0140
0.0125
0.0115
0.0143
0.0142
0.0126
0.0119
0.0126
0.0171
0.0128
0.0122
0.0118
0.0120
0.0117
0.0132
0.0123
0
0
0.0000
0.0000
0.0000
0.0000
0.0001
0.0002
0.0000
0.0000
0.0006
0.0002
0.0000
0.0000
0.0006
0.0002
0.0000
0.0000
0.0011
0.0010
0.0005
0.0001
0.0000
0.0011
0.0009
0.0003
0.0004
0.0002
0.0051
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.00000
0.00000
< MDL
< MDL
< MDL
< MDL
0.8
2.0
< MDL
< HDL
4.7
1.6
< MDL
< MDL
4.9
1.8
< HDL
< MDL
8.7
7.7
3.9
0.8
< HDL
8.6
7.0
2.3
3.1
1.5
41.0
< HDL
< MDL
< MDL
< MDL
< HDL
< MDL
< MDL
no sample
no sample
-------
TEST: PARTICIPATE tl
DATE: 06-19-92 AN
METHOD: NIOSH 500
GRID CHART - PARTICULATE
Painter Over
41.0
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
< MDL
PAINT TYPE: UNITE TOPCOAT
OBJECT: LADDERS
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
UNITS: «g/H3 GRID MDL: 0.1 iig/SAMPLE
OSHA TWA: 40 ng/IO PAINTER MDL: 0.1 •g/SAMPLE
D E INITIALS: BN I LJL
0 A INITIALS: LJL
1 2 3
< MDL < MDL < MDL
567
0.8 2.0 < HDL
9 10 11
4.7 1.6 < MDL
21 22 23
4.9 1.8 < MDL
13 14 15
8.7 3.9 0.8
7.7
17 18 19
8.6 7.0 3.1
2.3
4
< MDL
8
< MDL
12
< MDL
24
< MDL
16
< MDL
20
1.5
INLET GRID B
IB
< MDL
2B
< HDL
3B
< MDL
EXHAUST DUCT:no Maple
RECIRC DUCT:no Maple
-------
TEST: PARTIGUIATE 92
DATE: 06-19-92 PM
METHOD: NIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER
OBJECT: BOWSER
0 E INITIALS: BN I LJL
0 A INITIALS: LJL
ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE * FILTER ff PUMP * (nl/nin) (ml/min) (min)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
23DUP
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
2A DUP
3A
1B
2B
3B
F BLANK
EXHAUST
RECIRC
900109
900110
900111
900112
900113
900114
900115
900116
900117
900118
900119
900120
900121
900122
900123
900134
900124
900125
900126
900127
900128
900129
900130
900131
900132
900138
900139
900103
900104
900133
900105
900106
900107
900108
900135
26
124
173
70
153
61
184
3
77
90
178
206
201
207
51
98
164
200
30
59
57
129
136
183
65
195
43
93
80
62
39
38
45
180
163
33
36
25
20
16
1
24
12
29
4
22
13
32
6
18
5
14
31
30
19
9
35
34
26
11
28
21
3
10
23
7
8
15
27
2
3039
3060
3060
3066
3063
3018
3045
3088
3021
3085
3088
3048
3018
3036
3045
3036
3039
3045
3003
3012
3027
3000
3003
3057
3039
3006
3000
3024
3030
3085
3048
3045
3018
3012
3024
3094
3129
3051
3142
3033
3148
3164
3012
3057
3216
3714
3003
3027
3021
3024
3085
3003
3006
3009
3027
2994
2977
3051
3088
3024
2985
3003
3126
3174
3132
3082
3129
2994
38
38
38
38
38
39
38
38
38
38
34
37
38
38
38
39
38
38
38
38
40
38
38
5
39
37
37
41
42
37
39
42
45
41
38
PRE *1
(9)
0.0123
0.0123
0.0122
0.0117
0.0134
0.0115
0.0128
0.0131
0.0116
0.0115
0.0131
0.0119
0.0136
0.0121
0.0126
0.0115
0.0127
0.0125
0.0124
0.0134
0.0135
0.0138
0.0122
0.0120
0.0125
0.0131
0.0122
0.0125
0.0116
0.0125
0.0126
0.0135
0.0124
0.0121
0.0132
PRE »2
(g)
0.0123
0.0122
0.0122
0.0117
0.0133
0.0115
0.0128
0.0131
0.0116
0.0115
0.0131
0.0119
0.0136
0.0120
0.0126
0.0115
0.0128
0.0125
0.0124
0.0134
0.0135
0.0138
0.0122
0.0119
0.0124
0.0131
0.0121
0.0125
0.0116
0.0125
0.0125
0.0134
0.0124
0.0121
0.0132
POST *1
(9)
0.0122
0.0123
0.0121
0.0118
0.0134
0.0116
0.0129
0.0133
0.0118
0.0123
0.0139
0.0126
0.0140
0.0129
0.0138
0.0124
0.0136
0.0127
0.0133
0.0144
0.0145
0.0139
0.0125
0.0119
0.0136
0.0133
0.0121
0.0125
• 0.0116
0.0124
0.0126
0.0136
0.0124
0.0130
0.0132
POST #2 AVG FLOW
(9) (L/MIN)
0.0123 3.032
0.0122 3.077
0.0122 3.095
0.0117 .059
0.0134 .103
0.0116 .026
0.0129 .097
0.0133 .126
0.0118 .017
0.0123 3.071
0.0138 3.152
0.0126 3.381
0.0139 3.011
0.0128 3.032
0.0138 3.033
0.0124 3.030
0.0136 3.062
0.0127
0.0133
0.0143
0.0145
0.0139
0.0125
0.0120
0.0137
0.0132
0.0121
0.0125
0.0116
0.0124
0.0125
0.0134
0.0123
0.0130
0.0131
.024
.005
.011
.027
.997
.990
.054
.064
.015
.993
.014
.078
.130
.090
.064
.074
.003
.000
0.000
0.000
PRE AVG POST AVG
(g) (g)
0.0123
0.0122
0.0122
0.0117
0.0134
0.0115
0.0128
0.0131
0.0116
0.0115
0.0131
0.0119
0.0136
0.0121
0.0126
0.0115
0.0128
0.0125
0.0124
0.0134
0.0135
0.0138
0.0122
0.0119
0.0124
0.0131
0.0121
0.0125
0.0116
0.0125
0.0125
0.0135
0.0124
0.0121
0.0132
0.0000
0.0000
0.0122
0.0122
0.0122
0.0117
0.0134
0.0116
0.0129
0.0133
0.0118
0.0123
0.0139
0.0126
0.0139
0.0129
0.0138
0.0124
0.0136
0.0127
0.0133
0.0143
0.0145
0.0139
0.0125
0.0120
0.0136
0.0132
0.0121
0.0125
0.0116
0.0124
0.0125
0.0135
0.0123
0.0130
0.0131
0.0000
0.0000
PART WT PARTICULA
(g) (mg/M3)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0001
0.0002
0.0002
0.0008
0.0008
0.0007
0.0003
0.0008
0.0012
0.0009
0.0008
0.0002
0.0009
0.0009
0.0010
0.0001
0.0003
0.0001
0.0012
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0009
0.0000
0.0000 r
0.0000 r
< MDL
< MDL
< MDL
< MDL
< MDL
0.8
0.8
1.7
1.7
6.9
7.5
5.6
2.6
6.9
10.4
7.6
6.9
1.7
7.9
7.9
8.3
0.9
2.6
6.5
10.0
0.9
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
7.3
< MDL
to ample
w sanple
-------
TEST: PART ICULATE 02
DATE: 06-19-92 PH
METHOD: NIOSH 500
GRID CHART - PART ICULATE
Painter Over
0.9
Painter Under
< HDL
INLET GRID A
1A
< MDL
2A
< MDL
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
PAINT TTPE: LT GREEN PRIMER
OBJECT: BOUSER
UNITS: *g/M3
OSHA TWA: 7? *g/W
GRID MDL: 0.1 ng/SAMPLE
PAINTER MDL: 0.1 ng/SAMPLE
D E INITIALS: BN I LJL
0 A INITIALS: LJL
1
< MDL
5
< MDL
9
1.7
21
2.6
13
1.7
17
0.9
234
< MDL < MDL < MDL
678
0.8 0.8 1.7
10 11 12
6.9 7.5 5.6
22 23 24
6.9 10.4 6.9
7.6
14 15 16
7.9 7.9 8.3
18 19 20
2.6 6.5 10.0
Field Blank
< MDL
INLET GRID B
IB
< HDL
2B
< MDL
7.3
EXHAUST DUCT:no Maple
RECIRC DUCT:no sample
-------
TEST: PARTICULATE «3
DATE: 06-22-92 AM
METHOD: NIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: RED N20BASE 1 WHITE TOPCOAT
OBJECT: BOWSER & LADDERS
D E INITIALS: BN I LJL
0 A INITIALS: LJL
ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE * FILTER * PUMP * (ml/min) (ml/min) (min)
1
2
3
4
5
6
7
8
9
10
11
12
21
22
23
23 DUP
24
13
14
15
16
17
18
19
20
P over
P under
1A
2A
2A DUP
3A
IB
2B
3B
EXHAUST
RECIRC
900008
900009
900010
900011
900012
900013
900014
900015
900016
900017
900018
900018
900020
900021
900022
900032
900023
900024
900025
900026
900027
900028
900029
900030
900031
900066
900067
900001
900003
900007
900005
900002
900004
900006
63
148
12
11
73
166
195
76
1
109
192
105
58
115
8
132
36
215
27
14
74
46
123
99
208
150
50
64
144
83
32
199
41
149
8
6
25
1
41
12
33
4
7
5
14
2
10
26
30
22
24
31
9
42
16
36
11
23
43
21
32
13
3
20
27
29
40
19
3030
3048
3012
3015
3060
3030
3075
3072
3027
3063
3039
3066
3027
3066
3027
3204
3027
3066
3049
2985
3024
3066
3045
3030
3045
3051
3066
3060
3051
3082
3039
3027
3015
3027
2980
3021
3075
3066
3045
3085
3021
2997
3035
3033
2988
3012
3091
3119
2983
3204
3066
3000
3000
3030
3129
3110
2974
3151
2954
2400
2988
3097
3003
3021
3012
3000
2960
2950
70
72
71
73
72
72
71
71
72
73
72
55
73
1
72
62
72
72
75
71
71
71
72
72
72
70
70
70
70
70
70
69
69
69
PRE «1
(9)
0.0126
0.0124
0.0133
0.0125
0.0124
0.0133
0.0131
0.0127
0.0132
0.0122
0.0139
0.0134
0.0122
0.0123
0.0117
0.0136
0.0135
0.0130
0.0134
0.0134
0.0127
0.0132
0.0128
0.0116
0.0120
0.0128
0.0126
0.0126
0.0131
0.0126
0.0126
0.0130
0.0126
0.0125
PRE «2
(9)
0.0126
0.0123
0.0133
0.0125
0.0124
0.0134
0.0131
0.0127
0.0131
0.0122
0.0130
0.0135
0.0122
0.0123
0.0117
0.0135
0.0134
0.0130
0.0134
0.0134
0.0126
0.0132
0.0128
0.0116
0.0120
0.0128
0.0125
0.0126
0.0131
0.0126
0.0125
0.0130
0.0125
0.0125
POST *1
(9)
0.0126
0.0123
0.0134
0.0127
0.0125
0.0133
0.0133
0.0128
0.0120
0.0126
0.0140
0.0139
0.0124
0.0123
0.0129
0.0142
0.0144
0.0135
0.0141
0.0149
0.0131
0.0132
0.0141
0.0132
0.0132
0.0153
0.0126
0.0125
0.0131
0.0126
0.0125
0.0130
0.0116
0.0125
POST *2
(g)
0.0127
0.0123
0.0134
0.0127
0.0124
0.0134
0.0132
0.0128
0.0120
0.0126
0.0139
0.0139
0.0124
0.0122
0.0130
0.0142
0.0144
0.0135
0.0141
0.0149
0.0131
0.0133
0.0141
0.0132
0.0132
0.0153
0.0125
0.0125
0.0131
0.0126
0.0125
0.0129
0.0116
0.0125
AVG FLOW
(L/MIN)
3.005
3.035
3.044
3.041
3.053
3.058
3.048
3.035
3.031
3.048
3.014
3.039
3.059
3.093
3.005
3.204
3.047
3.033
3.025
3.008
3.077
3.088
3.010
3.091
3.000
2.726
3.027
3.079
3.027
3.052
3.026
3.014
2.988
2.989
0.000
0.000
PRE AVG POST AVG
(9) (0)
0.0126
0.0123
0.0133
0.0125
0.0124
0.0133
0.0131
0.0127
0.0132
0.0122
0.0135
0.0134
0.0122
0.0123
0.0117
0.0135
0.0135
0.013
0.0134
0.0134
0.0127
0.0132
0.0128
0.0116
0.012
0.0128
0.0126
0.0126
0.0131
0.0126
0.0125
0.013
0.0125
0.0125
0
0
0.0126
0.0123
0.0134
0.0127
0.0125
0.0133
0.0132
0.0128
0.012
0.0126
0.0139
0.0139
0.0124
0.0122
0.0129
0.0142
0.0144
0.0135
0.0141
0.0149
0.0131
0.0132
0.0141
0.0132
0.0132
0.0153
0.0126
0.0125
0.0131
0.0126
0.0125
0.013
0.0116
0.0125
0
0
PART WT
(9)
0.0000
0.0000
0.0001
0.0002
0.0001
0.0000
0.0001
0.0001
0.0000
0.0004
0.0004
0.0005
0.0002
0.0000
0.0012
0.0007
0.0009
0.0005
0.0007
0.0015
0.0004
0.0000
0.0013
0.0016
0.0012
0.0025
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
PARTICULATE
(mg/M3)
< MDL
< MDL
0.5
0.9
0.5
< MDL
0.5
0.5
< MDL
1.8
1.8
3.0
0.9
< MDL
5.5
3.5
4.1
2.3
3.1
7.0
1.8
< MDL
6.0
7.2
5.6
13.1
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
no sample
no sample
-------
8
TEST: PARTICULATE «3
DATE: 06-22-92 AM
METHOD: NIOSH 500
GRID CHART - PARTICULATE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: BN & LJL
0 A INITIALS: LJL
Painter Over
13.1
Painter Under
< HDL
INLET GRID A
1A
< MDL
2A
< MDL
< MDL
3A
< MDL
EXHAUST GRID
1 2 3 4
< MDL < MDL 0.5 0.9
5678
0.5 < MDL 0.5 0.5
9 10 11 12
< MDL 1.8 1.8 3.0
21 22 23 24
0.9 < MDL 5.5 4.1
3.5
13 14 15 16
2.3 3.1 7.0 1.8
17 18 19 20
< MDL 6.0 7.2 5.6
INLET GRID B
IB
< MDL
2B
< HDL
38
< HDL
PAINT TYPE: RED H20BASE t WHITE TOPCOAT UNITS: •g/tt GRID MDL: 0.1 Mg/SAMPLE
OBJECT: BOWSER I LADDERS OSHA TWA: 7? mg/M PAINTER HDL: 0.1 M0/SAMPLE
EXHAUST DUCT:no sample
RECIRC DUCT:no sample
-------
TEST: PARTICULATE *4
DATE: 06-24-92 AN
METHOD: NIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: BLUE UATERBASEO
OBJECT: COMFORT PALLET
D E INITIALS: BN 1 LJL
0 A INITIALS: LJL
ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE * FILTER * PUMP * (ml/min) (ml/min) (min)
1
2
3
4
5
6
7
8
9
9 OUP
10
11
12
12 DUP
21
22
23
24
13
14
15
15 DUP
16
17
18
18 DUP
19
20
P over
P under
1A
2A
3A
1B
2B
38
3B DUP
F BLANK
EXHAUST
RECIRC
900040
900041
900042
900043
900044
900045
900046
900047
900048
900049
900050
900051
900052
900053
900140
900064
900211
900065
900054
900055
900056
900057
900058
900059
900060
900061
900062
900063
900069
900070
900033
900034
900035
900036
900037
900038
900039
900068
18
165
42
54
189
91
172
101
168
86
210
56
154
139
194
137
79
47
37
15
25
34
89
171
55
100
96
126
188
118
205
97
131
19
141
179
186
13
10
14
2
17
22
19
36
37
6
41
40
4
31
33
34
30
16
11
15
21
24
8
20
5
18
1
25
42
28
32
7
43
3
29
35
27
12
26
3051
2994
2975
3051
3009
3051
3015
3069
3042
3009
3048
3079
3048
3045
3051
3003
3027
2997
2997
3027
3000
3074
3018
3057
3048
2974
3003
3079
3006
3069
2988
3057
3039
3079
3070
3051
2991
3030
3033
3003
3042
3069
3097
3110
3100
3042
2942
3045
3036
3003
3063
3036
3006
3072
3045
3006
3030
3039
3066
3063
3072
3006
2925
3018
3069
2991
3015
2945
3060
3000
3024
3051
3036
3018
70
70
54
70
61
70
70
70
70
71
70
70
70
70
70
70
70
71
70
70
70
71
70
71
70
71
70
70
69
69
70
69
69
69
69
69
69
69
PRE #1
(9)
0.0122
0.0132
0.0122
0.0115
0.0125
0.0125
0.0119
0.0117
0.0130
0.0130
0.0123
0.0126
0.0133
0.0118
0.0131
0.0119
0.0118
0.0126
0.0122
0.0124
0.0125
0.0124
0.0117
0.0122
0.0118
0.0121
0.0122
0.0124
0.0121
0.0133
0.0120
0.0117
0.0133
0.0123
0.0129
0.0130
0.0121
0.0122
PRE *2
(9)
0.0122
0.0132
0.0121
0.0115
0.0125
0.0125
0.0118
0.0117
0.0130
0.0130
0.0122
0.0126
0.0133
0.0118
0.0130
0.0119
0.0118
0.0125
0.0122
0.0124
0.0124
0.0124
0.0117
0.0120
0.0118
0.0121
0.0122
0.0124
0.0121
0.0133
0.0121
0.0118
0.0133
0.0122
0.0129
0.0130
0.0121
0.0122
POST *1
(9)
0.0122
0.0132
0.0123
0.0121
0.0125
0.0127
0.0129
0.0127
0.0134
0.0134
0.0133
0.0148
0.0151
0.0133
0.0135
0.0129
0.0141
0.0151
0.0126
0.0132
0.0142
0.0139
0.0135
0.0123
0.0124
0.0129
0.0147
0.0152
0.0150
0.0132
0.0121
0.0118
0.0133
0.0123
0.0129
0.0131
0.0121
0.0122
POST #2
(9)
0.0122
0.0132
0.0124
0.0120
0.0126
0.0127
0.0128
0.0127
0.0135
0.0134
0.0133
0.0149
0.0150
0.0134
0.0134
0.0129
0.0142
0.0151
0.0126
0.0131
0.0141
0.0139
0.0135
0.0213
0.0124
0.0129
0.0147
0.0152
0.0150
0.0132
0.0121
0.0118
0.0133
0.0123
0.0129
0.0130
0.0120
0.0122
AVG FLOW
(L/NIN)
3.041
3.014
2.989
3.047
3.039
3.074
3.063
3.085
3.042
2.976
3.047
3.058
3.026
3.054
3.044
3.005
3.050
3.021
3.002
3.029
3.020
3.070
3.041
3.065
3.027
2.950
3.011
3.074
2.999
3.042
2.967
3.059
3.020
3.052
3.061
3.044
3.005
3.000
0
0
PRE AVG POST AVG
(9) (9)
0.0122
0.0132
0.0121
0.0115
0.0125
0.0125
0.0119
0.0117
0.0130
0.0130
0.0122
0.0126
0.0133
0.0118
0.0130
0.0119
0.0118
0.0125
0.0122
0.0124
0.0124
0.0124
0.0117
0.0121
0.0118
0.0121
0.0122
0.0124
0.0121
0.0133
0.0121
0.0117
0.0133
0.0123
0.0129
0.0130
0.0121
0.0122
0.0000
0.0000
0.0122
0.0132
0.0124
0.0121
0.0125
0.0127
0.0128
0.0127
0.0134
0.0134
0.0133
0.0148
0.0151
0.0133
0.0135
0.0129
0.0142
0.0151
0.0126
0.0132
0.0141
0.0139
0.0135
0.0168
0.0124
0.0129
0.0147
0.0152
0.0150
0.0132
0.0121
0.0118
0.0133
0.0123
0.0129
0.0130
0.0121
0.0122
0.0000
0.0000
PART UT
(9)
0.0000
0.0000
0.0003
0.0006
0.0000
0.0002
0.0009
0.0010
0.0004
0.0004
0.0011
0.0022
0.0018
0.0015
0.0005
0.0010
0.0024
0.0026
0.0004
0.0008
0.0017
0.0015
0.0018
0.0047
0.0006
0.0008
0.0025
0.0028
0.0029
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
PARTICULA
(mg/M3)
< MDL
< MDL
1.9
2.8
< MDL
0.9
4.2
4.6
1.9
1.9
5.2
10.3
8.5
7.0
2.3
4.8
11.2
12.1
1.9
3.8
8.0
6.9
8.5
21.6
2.8
3.8
11.9
13.0
14.0
< HDL
< MDL
0.5
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
no sanplt
no ample
-------
TEST: PARTIOJLATE #4
DATE: 06-24-92 AN
METHOD: NIOSH 500
GRID CHART - PARTICIPATE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
0 E INITIALS: BN & LJL
0 A INITIALS: LJL
Painter Over
14.0
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
0.5
3A
< MDL
EXHAUST GRID
1234
< MDL < MDL 1.9 2.8
5 A 7 A
< MDL 0.9 4.2 4.6
9 10 11 12
1.9 5.2 10.3 8.5
1.9 7.0
21 22 23 24
2.3 4.8 11.2 12.1
13* 14 15 16
1.9 3.8 8.0 8.5
6.9
17 18 19 20
21.6 2.8 11.9 13.0
3.8
Field Blank
< MDL
INLET GRID B
1B
< MDL
28
< MDL
3B
< HDL
< MDL
PAINT TYPE: BLUE UATERBASED
OBJECT: COMFORT PALLET
UNITS: «g/M3 GRID MDL: 0.1 ng/SAMPLE
OSHA TWA: ?? ng/N3 PAINTER HDL: 0.1 «g/SAMPLE
EXHAUST DUCT: < HDL
RECIRC DUCT: < MDL
-------
TEST: PARTICULATE f5
DATE: 06-29-93 PM
METHOD: NIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER
OBJECT: QEC PANELS
D E INITIALS: BN I LJL
0 A INITIALS: LJL
10
ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE f FILTER * PUMP f (ml/min) (ml/min) (min)
1
2
3
4
5
6
6 DUP
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
20 DUP
P over
P under
1A
2A
3A
IB
IB DUP
2B
3B
F BLANK
EXHAUST
RECIRC
900151
900152
900153
900154
900155
900156
900157
900158
900159
900160
900161
900162
900163
900164
900165
900166
900167
900168
900169
900170
900171
900172
900173
900174
900175
900176
900141
900142
900144
900145
900146
900147
900148
900149
900150
900143
108
175
145
114
212
135
156
176
110
120
66
23
182
119
60
159
20
122
181
167
146
81
155
112
198
121
35
140
128
202
211
113
197
190
191
170
55
42
54
25
49
47
19
12
35
33
32
46
30
48
51
29
34
18
20
45
53
50
21
40
17
15
31
52
28
43
16
14
4
1
7
3
3010
3000
3024
3000
3060
3060
3035
3002
3036
3040
3060
3000
3033
3035
3000
3003
3006
3010
3040
3068
3050
3050
3045
3040
3045
3015
3030
3050
3040
2990
3060
2980
2975
2990
2960
3033
3033
2994
2997
3085
3075
3003
3040
3006
3069
3069
3051
3021
3103
3015
2985
2968
3048
3033
3048
3033
3033
3045
3082
3021
3015
2985
3027
3012
3024
3119
3012
2884
3033
2887
68
68
68
68
68
68
68
68
68
68
68
68
68
67
68
68
68
68
68
68
68
67
68
68
68
69
67
68
67
67
67
68
67
68
68
68
PRE *1
(9)
0.0122
0.0126
0.0130
0.0117
0.0131
0.0128
0.0129
0.0133
0.0136
0.0122
0.0123
0.0135
0.0127
0.0125
0.0130
0.0119
0.0117
0.0134
0.0128
0.0130
0.0120
0.0120
0.0133
0.0131
0.0128
0.0133
0.0125
0.0132
0.0127
0.0120
0.0127
0.0124
0.0139
0.0125
0.0130
0.0119
PRE «2
<9>
0.0122
0.0127
0.0129
0.0117
0.0132
0.0128
0.0129
0.0132
0.0135
0.0123
0.0124
0.0135
0.0127
0.0125
0.0130
0.0119
0.0117
0.0134
0.0128
0.0130
0.0120
0.0121
0.0133
0.0131
0.0129
0.0132
0.0124
0.0131
0.0127
0.0120
0.0127
0.0124
0.0138
0.0125
0.0130
0.0120
POST *1
(9)
0.0123
0.0127
0.0129
0.0117
0.0131
0.0127
0.0128
0.0133
0.0136
0.0123
0.0124
0.0136
0.0127
0.0125
0.0131
0.0122
0.0118
0.0135
0.0129
0.0133
0.0121
0.0122
0.0134
0.0134
0.0130
0.0132
0.0126
0.0132
0.0127
0.0119
0.0126
0.0124
0.0138
0.0125
0.0130
0*0120
POST #2
(9)
0.0123
0.0126
0.0129
0.0117
0.0131
0.0127
0.0129
0.0133
0.0135
0.0123
0.0124
0.0136
0.0127
0.0125
0.0131
0.0122
0.0118
0.0134
0.0130
0.0133
0.0121
0.0122
0.0135
0.0133
0.0130
0.0133
0.0127
0.0131
0.0126
0.0119
0.0125
0.0124
0.0138
0.0125
0.0130
0.0119
AVG FLOW
(L/NIN)
3.022
3.017
3.009
2.999
3.073
3.068
3.019
3.021
3.021
3.055
3.065
3.026
3.027
3.069
3.008
2.994
2.987
3.029
3.037
3.058
3.042
3.042
3.045
3.061
3.033
3.015
3.008
3.039
3.026
3.007
3.090
2.996
2.930
3.012
2.924
3.000
0.000
0.000
PRE AVG POST AVG
(g) (g)
0.0122
0.0127
0.0130
0.0117
0.0131
0.0128
0.0129
0.0132
0.0136
0.0123
0.0123
0.0135
0.0127
0.0125
0.0130
0.0119
0.0117
0.0134
0.0128
0.0130
0.0120
0.0121
0.0133
0.0131
0.0129
0.0133
0.0125
0.0132
0.0127
0.0120
0.0127
0.0124
0.0138
0.0125
0.0130
0.0119
0.0000
0.0000
0.0123
0.0127
0.0129
0.0117
0.0131
0.0127
0.0129
0.0133
0.0135
0.0123
0.0124
0.0136
0.0127
0.0125
0.0131
0.0122
0.0118
0.0134
0.0130
0.0133
0.0121
0.0122
0.0134
0.0133
0.0130
0.0133
0.0126
0.0131
0.0127
0.0119
0.0126
0.0124
0.0138
0.0125
0.0130
0.0120
0.0000
0.0000
PART UT
(9)
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0001
0.0001
0.0000
0.0000
0.0001
0.0003
0.0001
0.0000
0.0002
0.0003
0.0001
0.0001
0.0001
0.0002
0.0001
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
PARTICULATE
-------
TEST: PARTICULATE «5
DATE: 06-29-92 PM
METHOD: NIOSH 500
GRID CHART - PARTICULATE
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: BN t LJL
0 A INITIALS: LJL
Painter Over
0.5
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< HDL
3A
< MDL
EXHAUST GRID
1234
0.5 < MDL < MDL < MDL
5678
< MDL < MDL 0.5 < MDL
< MDL
9 10 11 12
< MDL 0.5 0.5 < MDL
21 22 23 24
< MDL 0.5 1.5 0.5
13 14 15 16
< MDL 1.0 1.4 0.5
17 18 19 20
0.5 0.5 1.0 0.5
< MDL
Field Blank
0.5
INLET GRID B
1B
< MDL
< MDL
2B
< MDL
3B
< HDL
PAINT TYPE: LT GREEN PRIMER
OBJECT: PEC PANELS
UNITS: ng/W
OSHA TWA: 77 Mg/M3
GRID MDL: 0.1 *g/SAMPLE
PAINTER MDL: 0.1 HO/SAMPLE
EXHAUST DUCT:no
RECIRC DUCT:no tMpte
-------
TEST: SINGLE PASS PARTICUIATE t1
DATE: 07-01-92 AM2
METHOD: NIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: PRIMER I GRAY TOPCOAT
OBJECT: RAMP I OEC PANELS
0 E INITIALS: BN I LJL
0 A INITIALS: LJL
ACUREX
GRID LOG SAMPLE f FILTER
f PUMP *
(RAW DATA, BALANCE ACCURACY 0.0001)
PRE-CAL POST-CAL RUN TIME PRE «1 PRE «2 POST fl POST #2 AVG FLOW PRE AVG POST AVG PART UT PARTICULATE
((•I/Bin) (ml/pin) (nin) (9) (g) (g) (g) (L/MIN) (g) (g) (g) (Mg/M3)
1
2
3
3 DUP
4
5
6
7
B
9
10
11
11 DUP
12
21
22
22 OOP
23
24
13
14
15
15 DUP
16
17
18
19
20
P over
P under
1A
2A
3A
IB
28
38
F BLANK?
EXHAUST
RECIRC
900185
900186
900187
900214
900188
900189
900190
900191
900192
900193
900194
900195
900213
900196
900197
900198
900212
900199
900200
900201
900202
900203
900210
900204
900205
900206
900207
900208
900184
900183
900177
900178
900179
900180
900181
900182
68
213
46
44
75
125
10
7
48
117
138
87
187
177
127
143
52
104
169
103
107
95
204
130
142
174
4
78
106
182
196
161
72
111
147
158
45
11
28
53
43
29
33
51
18
24
19
17
35
5
42
7
31
54
50
30
20
13
55
47
34
IS
12
10
49
52
39
36
1
6
16
32
3009
3009
2957
2994
2991
3000
3009
2994
3027
3003
2991
3009
2968
3027
2994
2965
2977
2983
3033
3000
2980
3030
3006
3000
3009
2968
3006
3015
2983
3036
2985
2985
2968
3018
2977
2994
3033
3033
2968
3030
2980
2994
2957
3006
3003
3060
2977
3015
2983
3018
3030
2971
2940
2985
2998
2994
2974
2991
3012
2988
3009
2983
3048
3110
2925
3012
2994
3042
2934
3009
3000
2977
62
63
62
62
62
62
62
62
62
62
62
62
1
63
62
62
63
62
62
62
62
61
62
62
62
63
62
63
62
62
61
61
62
62
62
61
0.0133
0.0128
0.0132
0.0116
0.0126
0.0127
0.0123
0.0121
0.0132
0.0121
0.0123
0.0117
0.0123
0.0127
0.0133
0.0133
0.0127
0.0126
0.0131
0.0128
0.0136
0.0125
0.0120
0.0121
0.0133
0.0126
0.0117
0.0127
0.0124
0.0127
0.0129
0.0125
0.0120
0.0134
0.0124
0.0122
0.0133
0.0128
0.0132
0.0116
0.0127
0.0127
0.0123
0.0121
0.0131
0.0121
0.0124
0.0117
0.0123
0.0126
0.0133
0.0133
0.0127
0.0126
0.0131
0.0128
0.0135
0.0125
0.0120
0.0122
0.0133
0.0126
0.0116
0.0127
0.0125
0.0127
0.0129
0.0124
0.0120
0.0133
0.0124
0.0122
0.0133
0.0128
0.0132
0.0116
0.0127
0.0128
0.0124
0.0122
0.0132
0.0123
0.0128
0.0123
0.0123
0.0130
0.0136
0.0140
0.0130
0.0135
0.0134
0.0132
0.0153
0.0140
0.0134
0.0125
0.0153
0.0148
0.0137
0.0137
0.0123
0.0127
0.0130
0.0124
0.0120
0.0134
0.0124
0.0122
0.0133
0.0128
0.0133
0.0116
0.0127
0.0127
0.0124
0.0122
0.0132
0.0124
0.0128
0.0123
0.0123
0.0129
0.0135
0.0139
0.0129
0.0135
0.0133
0.0132
0.0153
0.0140
0.0134
0.0124
0.0152
0.0149
0.0137
0.0137
0.0123
0.0127
0.0129
0.0124
0.0120
0.0133
0.0123
0.0121
3.021
3.021
2.963
3.012
2.986
2.997
2.983
3.000
3.015
3.032
2.984
3.012
2.976
3.023
3.012
2.968
2.959
2.984
3.016
2.997
2.977
3.011
3.009
2.994
3.009
2.976
3.027
3.063
2.954
3.024
2.990
3.014
2.951
3.014
2.989
2.986
0.000
0.000
0.000
0.0133
0.0128
0.0132
0.0116
0.0126
0.0127
0.0123
0.0121
0.0131
0.0121
0.0123
0.0117
0.0123
0.0127
0.0133
0.0133
0.0127
0.0126
0.0131
0.0128
0.0135
0.0125
0.0120
0.0121
0.0133
0.0126
0.0117
0.0127
0.0125
0.0127
0.0129
0.0124
0.0120
0.0134
0.0124
0.0122
0.0000
0.0000
0.0000
0.0133
0.0128
0.0132
0.0116
0.0127
0.0128
0.0124
0.0122
0.0132
0.0124
0.0128
0.0123
0.0123
0.0129
0.0136
0.0139
0.0130
0.0135
0.0134
0.0132
0.0153
0.0140
0.0134
0.0124
0.0152
0.0148
0.0137
0.0137
0.0123
0.0127
0.0129
0.0124
0.0120
0.0133
0.0123
0.0121
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0001
0.0001
0.0001
0.0001
0.0003
0.0005
0.0006
0.0000
0.0002
0.0003
0.0006
0.0003
0.0009
0.0003
0.0004
0.0018
0.0015
0.0014
0.0003
0.0019
0.0022
0.0020
0.0010
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
< NDL
< MDL
< MDL
< MDL
0.5
0.5
0.5
0.5
0.5
1.6
2.7
3.2
< NDL
1.1
1.6
3.3
1.6
4.9
1.6
2.2
9.8
8.2
7.5
1.6
10.2
11.7
10.7
5.2
< MDL
< MDl
< MDL
< MDl
< MDL
< MDL
< MDL
< MDL
no Mplo
no Mopl*
no iMpl*
-------
tn
TEST: SINGLE PASS PARTICIPATE fl
DATE: 07-01-92 AM2
METHOD: MIOSH 500
GRID CHART - PARTICULATE
Pafnter Over
< HDL
Painter Under
< HDL
INLET GRID A
1A
< HDL
2A
< HDL
3A
< HDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
PAIHT TYPE: PRIHER I 6RAT TOPCOAT UNITS: HO/MS GRID HDL: 0.1 •g/SAHPLE
OBJECT: RAHP t OEC PANELS OSHA TWA: 77 MB/lO PAINTER HDL: 0.1 MB/SAMPLE
D E INITIALS: BN I LJL
0 A INITIALS: LJL
1
< HDL
5
O.S
9
1.6
21
1.6
13
2.2
17
10.2
234
< HDL < HDL 0.5
< HDL
678
O.S 0.5 0.5
10 11 12
2.7 3.2 1.1
< HDL
22 23 24
3.3 4.9 1.6
1.6
14 15 16
9.8 8.2 1.6
7.5
18 19 20
11.7 10.7 5.2
Field Blank
IHLET GRID B
18
< HDL
< HDL
< HDL
EXHAUST OUCTtno Maple
RECIRC OUCT:no Maple
-------
TEST: S.P. PARTICUlATE *2
DATE: 07-01-92 PN
METHOD: MIOSH 500
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: GRAY TOPCOAT
OBJECT: BOX, PIPES i TABLE
D E INITIALS: BN t LJL
0 A INITIALS: LJL
CO
ACUREX PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE f FILTER ff PUMP » («l/«rin) (nl/nin) (rain)
1
2
2 DUP
3
4
5
6
7
8
9
10
11
12
12 DUP
21
22
22 DUP
23
24
13
14
15
16
16 DUP
17
18
19
20
P over
P infer
1A
2A
3A
IB
28
38
f BLANK?
EXHAUST
RECIRC
900209
900215
900216
900217
900218
900219
900220
900221
900222
900223
900224
900225
900226
900227
900228
900229
900230
900231
900232
900233
900234
900235
900236
900237
900238
900239
900240
900241
900249
900250
900242
900244
900245
900246
900247
900248
249
216
236
255
246
251
240
230
219
234
229
252
221
244
241
217
220
237
232
233
225
222
247
253
227
245
235
254
243
224
250
248
231
239
238
218
55
15
24
18
39
11
1
43
28
53
10
29
30
50
35
7
5
34
42
33
6
47
54
20
17
16
45
36
52
49
31
32
19
13
12
51
3012
2983
3060
3003
2994
3033
3036
2980
2968
3030
3060
2994
2994
2998
2983
2971
3018
3009
3030
2957
3009
2988
2985
2974
3015
3000
3033
3042
3012
2974
2941
2977
2977
2991
3048
3006
2974
3033
3091
3000
3072
3129
2977
2986
2948
3048
3075
2895
2934
3027
2994
2965
3003
2988
3021
2959
3018
2957
2959
2954
2974
3054
3027
3042
3045
2980
2917
2912
2959
3033
3072
2974
67
68
68
68
68
68
68
68
68
68
68
68
68
68
67
68
69
68
68
68
68
68
68
68
67
67
68
68
68
67
67
67
67
66
68
68
PRE *1
(9)
0.0119
0.0128
0.0119
0.0121
0.0121
0.0127
0.0124
0.0129
0.0120
0.0134
0.0129
0.0133
0.0132
0.0121
0.0125
0.0122
0.0117
0.0119
0.0132
0.0131
0.0124
0.0129
0.0132
0.0123
0.0129
0.0123
0.0120
0.0127
0.0131
0.0123
0.0113
0.0126
0.0128
0.0123
0.0119
0.0117
PRE «2
(g)
0.0121
0.0128
0.0119
0.0123
0.0122
0.0130
0.0124
0.0129
0.0120
0.0134
0.0129
0.0134
0.0132
0.0124
0.0129
0.0121
0.0117
0.0119
0.0132
0.0131
0.0123
0.0128
0.0126
0.0124
0.0128
0.0124
0.0120
0.0130
0.0133
0.0123
0.0115
0.0126
0.0128
0.0125
0.0118
0.0117
POST f 1
(g)
0.0120
0.0127
0.0119
0.0124
0.0125
0.0131
0.0125
0.0131
0.0122
0.0137
0.0137
0.0144
0.0138
0.0128
0.0132
0.0131
0.0124
0.0133
0.0139
0.0134
0.0136
0.0144
0.0143
0.0131
0.0138
0.0140
0.0135
0.0136
0.0153
0.0129
0.0115
0.0126
0.0127
0.0124
0.0118
0.0117
POST *2
(g)
0.0120
0.0127
0.0119
0.0124
0.0124
0.0131
0.0125
0.0131
0.0122
0.0137
0.0136
0.0144
0.0139
0.0128
0.0131
0.0131
0.0125
0.0132
0.0139
0.0135
0.0136
0.0144
0.0143
0.0131
0.0137
0.0139
0.0134
0.0136
0.0154
0.0129
0.0114
0.0125
0.0127
0.0123
0.0117
0.0117
AVG FLOW
(L/MIN)
2.993
3.008
3.076
3.002
3.033
3.081
3.007
2.983
2.958
3.039
3.068
2.945
2.964
3.013
2.989
2.968
3.011
2.999
3.026
2.958
3.014
2.973
2.972
2.964
2.995
3.027
3.030
3.042
3.029
2.977
2.929
2.945
2.968
3.012
3.060
2.990
0.000
0.000
0.000
PRE AVG POST AVG
(g) (g)
0.0120
0.0128
0.0119
0.0122
0.0121
0.0129
0.0124
0.0129
0.0120
0.0134
0.0129
0.0134
0.0132
0.0122
0.0127
0.0121
0.0117
0.0119
0.0132
0.0131
0.0123
0.0128
0.0129
0,0124
0.0128
0.0123
0.0120
0.0128
0.0132
0.0123
0.0114
0.0126
0.0128
0.0124
0.0119
0.0117
0.0000
0.0000
0.0000
0.0120
0.0127
0.0119
0.0124
0.0125
0.0131
0.0125
0.0131
0.0122
0.0137
0.0137
0.0144
0.0138
0.0128
0.0131
0.0131
0.0124
0.0133
0.0139
0.0134
0.0136
0.0144
0.0143
0.0131
0.0137
0.0140
0.0135
0.0136
0.0153
0.0129
0.0114
0.0125
0.0127
0.0123
0.0118
0.0117
0.0000
0.0000
0.0000
PART VT
(g)
0.0000
0.0000
0.0000
0.0002
0.0004
0.0002
0.0001
0.0002
0.0002
0.0003
0.0008
0.0010
0.0006
0.0006
0.0004
0.0010
0.0007
0.0014
0.0007
0.0003
0.0013
0.0016
0.0014
0.0007
0.0009
0.0017
0.0015
0.0008
0.0021
0.0006
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
PARTICULA
(mg/M3)
< MDL
< MDL
< MDL
.0
.9
.0
.5
.0
.0
.5
.8
.0
.0
.9
.0
.0
.4
.9
.4
.5
.3
.9
.9
.5
.5
.4
7.3
3.9
10.2
3.0
< MDL
< HDL
< MDL
< MDL
< MDL
< HDL
no *Mpl«
no «Mpl«
no taopl*
-------
TEST: S.P. PARTICUIATE «2
DATE: 07-01-92 PN
NETHOO: NIOSH 500
GRID CHART - PARTICUIATE
Painter Over
10.2
Painter Under
3.0
INLET GRID A
1A
< MDL
2A
< NDL
3A
< NDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
PAINT TYPE: GRAY TOPCOAT
OBJECT: MM, PIPES ft TABLE
UNITS: mgflO
OSHA TUA: T? BQ/W
GRID NDL: 0.1 og/SAMPLE
PAINTER NDL: 0.1 HO/SAMPLE
D E INITIALS: BN t LJL
Q A INITIALS: LJL
1
< NDL
5
1.0
9
1.5
21
2.0
13
1.5
17
4.5
234
< NDL 1.0 1.9
< NDL
678
0.5 1.0 1.0
10 11 12
3.8 5.0 3.0
2.9
22 23 24
5.0 6.9 3.4
3.4
14 15 16
6.3 7.9 6.9
3.5
18 19 20
8.4 7.3 3.9
Field Blank
INLET GRID B
IB
< NDL
< NDL
NDL
EXHAUST DUCT:no Maple
RECIRC DUCT:no Maple
-------
TEST: METALS «1
DATE: 06-23-92 PM
METHOD: NIOSH 7300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT:
OBJECT:
IT GREEN PRIMER
COMFORT PALLET
D E INITIALS:
0 A INITIALS:
LJL
CO
ACUREX BASE PRE-CAL POST-CAL RUN TIME
GRID LOC SAMPLE * SAMPLE * PUMP * (ml/min) (nl/min) (nin)
1
2
3
4
5
6
7
8
9
10
11
12
12 OUP
21
22
23
24
13
14
15
15 OOP
16
17
18
19
20
f over
P under
1A
2A
3A
IB
2B
3B
P over *
P under*
BLANK
39 EX921067
18 EX921068
7 EX921069
26 EX921070
22 EX921071
24 EX921072
1 EX921073
15 EX921074
21 EX921075
6 EX921076
25 EX921077
78 EX921078
16 EX921091
40 EX921087
19 EX921088
27 EX921089
11 EX921090
10 EX921079
29 EX921080
4 EX921081
17 EX921092
77 EX921082
20 EX921083
23 EX921084
2 EX921085
12 EX921086
14 EX921127
9 EX921126
13 EX921061
30 EX921062
5 EX921063
3 EX921064
28 EX921065
8 EX921066
212 EX921279
213 EX921280
41
35
23
43
31
12
30
4
8
6
14
1
34
10
11
33
24
36
9
42
28
18
7
5
25
16
19
32
20
3
27
29
13
40
18
21
3045
3023
3042
2980
3000
3085
2983
2997
2980
3021
2988
3066
3006
3091
2974
3021
3066
3054
3000
2985
3045
3021
3006
3033
3075
3021
3003
2988
3021
3003
3012
3000
3097
3009
3024
3012
3039
2956
3036
2994
2994
3151
3003
2959
2988
3027
2903
3029
3000
3171
3042
3021
3158
3075
2926
2959
3012
2991
3063
3018
3129
3027
2957
2974
3012
3009
2994
2977
3280
3009
2988
2934
47 <
46 <
47 <
46 <
46 <
46 <
46 <
46 <
47 <
47 <
47 <
47 <
46 <
47 <
47 <
46 <
47
46
48 <
46 <
46 <
46 <
46 <
47 <
46
46
45 <
45 <
46 <
45 <
45 <
46 <
45 <
46 <
38 <
38 <
LEAD
(ug)
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.24
0.14
0.075
0.075
0.075
0.075
0.073
0.075
0.14
0.10
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
ZINC STRONTIUM CHROMIUM
(ug) (ug) (ug)
0.80
1.06
1.46
0.42
0.45
0.72
1.29
0.69
1.06
0.48
0.86
0.50 <
0.63
1.29
0.75
0.62
3.08
2.25
0.50
0.56
0.41
0.44
0.56
0.51
0.51
0.41
0.62
0.46
Q.42 <
0.62 <
0.48 <
0.48 <
0.64 <
0.44
0.58
0.58
0.80
1.72
7.47
15.88
2.37
6.06
16.11
24.92
5.78
24.34
31.50
0.30 <
57.57
8.12
26.12
59.14
72.09
12.58
40.12
33.16
30.64
70.80
3.52
16.68
82.44
142.46
51.22
6.78
0.30
0.30 <
0.30 <
0.30 <
0.30
0.45
60.14
14.52
0.57
1.22
4.52
9.63
1.50
3.64
9.50
14.68
3.54
14.37
18.80
0.30
33.82
5.06
15.81
36.16
42.58
7.44
24.22
19.54
18.41
42.48
3.36
10.23
49.35
81.94
30.21
4.26
1.18
0.30
0.30
0.30
1.86
0.39
35.28
8.60
AVG FLOW LEAD ZINC STRONTIUM CHROMIUM
(L/MIN) (ug/M3) (ug/M3) (ug/M3) (ug/M3)
3.042 < MDL
2.990 < MDL
3.039 < MDL
2.987 < MDL
2.997 < MDL
3.118 < MDL
2.993 < MDL
2.978 < HDL
2.984 < MDL
3.024 < MDL
2.946 < MDL
3.048 < MDL
3.003 < MDL
3.131 < MDL
3.008 < MDL
3.021 < MDL
3.112 1.6
3.065 1.0
2.963 < MDL
2.972 < MDL
3.029 < MDL
3.006 < MDL
3.035 < MDL
3.026 < MDL
3.102 1.0
3.024 0.7
2.980 < MDL
2.981 < HDL
3.017 < MDL
3.006 < MDL
3.003 < MDL
2.989 < MDL
3.189 < MDL
3.009 < MDL
3.006 < MDL
2.973 < MDL
0.000 no taapleno
5.6
7.7
10.2
3.1
3.3
5.0
9.4
5.0
7.6
3.4
6.2
3.5
4.6
8.8
5.3
4.5
21.1
16.0
3.5
4.1
2.9
3.2
4.0
3.6
3.6
2.9
4.6
3.4
3.0
4.6
3.6
3.5
4.5
3.2
5.1
5.1
5.6
12.5
52.3
115.6
17.2
42.3
117.0
181.9
41.2
171.3
227.5
< MDL
416.8
55.2
184.8
425.6
492.9
89.2
282.1
242.6
219.9
512.0
25.2
117.3
577.7
1024.1
382.0
50.5
< MDL
< MDL
< MDL
< MDL
< MDL
3.3
526.5
128.5
•Mpleno Mnpleno
4.0
8.9
31.6
70.1
10.9
25.4
69.0
107.2
25.2
101.1
135.8
< MDL
244.8
34.4
111.8
260.2
291.1
52.8
170.3
142.9
132.2
307.2
24.1
71.9
345.8
589.1
225.3
31.8
8.5
< MDL
< MDL
< MDL
13.0
2.8
308.9
76.1
sample
LOCATION
EXHAUST
RECIRC
SAMPLES
ACETONE NITRIC FILTER IMPINCER
EX921376 EX921377 EX921378 EX921379
EX921380 EX921381 EX921394 EX921395
EXHAUST ACETONE
NITRIC
FILTER
SAMPLE
(CU FT)
38.80
48.98
EX921376 <
EX921377 <
EX921378 <
LEAD
(ug)
0
2.5
2.5
0.5
2.5 <
ZINC J
(ug)
32.05
133
1.85
5.2
1.25
iTRONTIUM
(ug)
15.85
15.4
7.3
7.7
0.85
CHROMIUM
(ug)
25.4
87.4
4.50
7.20
1.70
SAMPLE
(N3)
1.098
1.386
1.098
1.098
1.098
LEAD
(ug/M3)
< MDL
1.8
< MDL
< MDL
< MDL
ZINC SI
(ug/M3) (
29.2
96.0
1.7
4.7
< MDL
RONTIUM (
!ug/M3) (
14.4
11.1
6.6
7.0
0.8
:HRONIUM
[ug/M3)
23.1
63.1
4.1
6.6
1.5
-------
TEST: METALS f1 TRAVIS AFB PAINT: IT GREEN PR I HER 0 E INITIALS: LJL
DATE: 06-22-93 PN PAINT BOOTH TESTS OBJECT: COMFORT PALLET Q A INITIALS:
METHOD: NIOSH 7300 ACUREX PROJECT 8485
ACUREX BASE - PRE-CAL POST-CAL RUN TIME LEAD ZINC STRONTIUM CHROMIUM AVG FLOW LEAD ZINC STRONTIUM CHROMIUM
GRID LOC SAMPLE * SAMPLE * PUMP * (nl/min) (ml/min) (min) (ug) (ug) (ug) (ug) (L/MIM) (ug/M3) (ug/M3) (ug/«) (ug/M3)
IMPINGER EX921379 < 0.5 25 < 0.2 12.00 1.098 < HDL 22.8 < MDL 10.9
RECIRC ACETONE EX921380 < 2.5 15 5.3 5.40 1.386 < MDL 10.8 3.8 3.9
NITRIC EX921381 < 1.0 60 8.5 26.00 1.386 < MDL 43.3 6.1 18.8
FILTER EX921394 2.5 18 1.6 44.00 1.386 1.8 13.0 1.2 31.7
IMPINGER EX921395 < 0.5 40 < 0.2 12.00 1.386 < MDL 28.9 < MDL 8.7
(O
-------
TEST: METALS *1
DATE: 06-22-92 PM
METHOD: NIOSH 7300
GRID CHART 1 - LEAD
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
< MDL
< HDL 2nd
Painter Under
< MDL
< MDL 2nd
INLET CHID A
1A
< MDL
2A
< MDL
3A
-------
10
TEST: METALS #1
DATE: 06-22-92 PM
METHOD: NIOSH 7300
GRID CHART 2 - ZINC
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
4.6
5.1 2nd
Painter Under
3.*
5.1 2nd
INLET GRID A
1A
3.0
2A
4.6
3A
3.6
EXHAUST GRID
1234
5.6 7.7 10.2 3.1
5678
3.3 5.0 9.4 5.0
9 10 11 12
7.6 3.4 6.2 3.5
4.6
21 22 23 24
8.8 5.3 4.5 21.1
13 14 15 16
16.0 3.5 4.1 3.2
2.9
17 18 19 20
4.0 3.6 3.6 2.9
PAINT TYPE: LT GREEN PRIMER UNITS: ug/W GRID MDL: 0.3 ug/SANPLE
EXHAUST I
INLET GRID B
1B
3.5
2B
4.5
38
3.2
lUCT: 29.2
OBJECT: COMFORT PALLET OSHA TWA: 1000 ug/W PAINTER MDL: 0.3 ug/SANPLE RECIRC DUCT: 96.0
-------
TEST: METALS *1
DATE: 06-22-92 PM
METHOD: NIOSH 7300
GRID CHART 3 - STRONTIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8465
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
382.0
526.5 2nd
Painter Under
50.5
128.5 2nd
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
5.6 12.5 52.3 115.6
c 67 8
17.2 42.3 117.0 181.9
9 10 11 12
41.2 171.3 227.5 < MDL
416.8
21 22 23 24
55.2 184.8 425.6 492.9
13 14 15 16
89.2 282.1 242.6 512.0
219.9
17 18 19 20
25.2 117.3 577.7 1024.1
INLET GRID B
IB
< MDL
2B
< MDL
3B
3.3
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: COMFORT PALLET OSHA TWA: 7? ug/M3
GRID MDL: 0.3 ug/SAMPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 14.4
RECIRC DUCT: 11.1
-------
TEST: METALS *1
DATE: 06-23-92 PM
METHOD: NIOSH 7300
GRID CHART 4 - CHROMIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
225.3
308.9 2nd
Painter Under
31.8
76.1 2nd
INLET GRID A
1A
8.5
2A
< NDL
3A
< NDL
EXHAUST GRID
1 2 34
4.0 8.9 31.6 70.1
5678
10.9 25.4 69.0 107.2
9 10 11 12
25.2 101.1 135.8 < NDL
244.8
21 22 23 24
34.4 111.8 260.2 291.1
13 14 15 16
52.8 170.3 142.9 307.2
132.2
17 18 19 20
24.1 71.9 345.8 589.1
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3 GRID NDL: 0.3 ug/SAMPLE
EXHAUST C
INLET GRID B
1B
< MDL
2B
13.0
3B
2.8
IUCT: 23.1
OBJECT: COMFORT PALLET OSHA TWA: 50 ug/M3 PAINTER NDL: 0.3 ug/SAMPLE RECIRC DUCT: 63.1
-------
TEST: METALS «2
DATE: 06-24-92 PM
METHOD: N10SH 7300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER
OBJECT: SPLITTERS
D E INITIALS:
0 A INITIALS:
ACUREX BASE
GRID LOG SAMPLE * SAMPLE *
1
2
2 DUP
3
4
5
6
7
8
9
10
11
12
21
22
23
23 DUP
24
13
14
14 DUP
15
16
17
18
19
20
P over
P under
1A
2A
3A
3A DUP
1B
2B
3B
FLO BLANK
LOCATION
EXHAUST
RECIRC
120 EX921097
69 EX921098
79 EX921099
89 EX921100
91 EX921101
92 EX921102
45 EX921103
50 EX921104
47 EX921105
118 EX921106
34 EX921107
83 EX921108
95 EX921109
36 EX921110
31 EX921111
37 EX921112
35 EX921113
90 EX921114
43 EX921115
41 EX921116
99 6X921117
88 EX921118
94 EX921119
44 EX921120
108 EX921121
107 EX921122
93 EX921123
32 EX921124
33 EX921125
46 EX921093
42 EX921094
38 EX921095
49 EX921096
113 EX921128
48 EX921129
103 EX921130
104 EX921271
SAMPLES
ACETONE
EX921382
EX921386
PUMP *
15
40
13
25
31
34
19
4
11
6
30
24
20
10
1
8
7
42
5
14
18
16
33
41
21
36
23
32
35
28
43
3
26
12
29
27
9
NITRIC
EX9213B3
EX921387
PRE-CAL POST-CAL RUN TIME
(ml/mi n) (ml/min) (rain)
3006 3054 66 <
3045 3021 66 <
3066 3129 64 <
3018 3082 66 <
3003 2980 66 <
3036 2991 65 <
3021 3006 66 <
3036 3015 66
3045 3088 66
3042 3000 66 <
3006 2985 66 <
3039 3119 66 <
3063 3042 66 <
3030 3091 66 <
3039 3088 67
3066 3049 67 <
3020 3036 66 <
3069 3042 66 <
3072 3036 66 <
3033 3003 66
3066 3018 66
3072 3129 66
3063 3033 66
3021 3012 66
3030 3003 66
3042 3066 66 <
3036 3224 66
3015 2942 65
3051 3027 65 <
2991 3006 65 <
3060 3054 65 <
3000 2985 65 <
2985 2968 1 <
3018 3090 65 <
3024 2962 65 <
3036 2983 65 <
66 <
SAMPLE
FILTER INPINGER (CU FT)
EX921384 EX921385 39.20
EX921416 EX921417 40.84
EXHAUST ACETONE EX921382 <
NITRIC EX921383 <
FILTER EX921384 <
IMPINGER EX921385 <
LEAD
(ug)
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.077
0.077
0.075
0.075
0.075
0.075
0.075
0.079
0.075
0.075
0.075
0.075
0.075
0.075
0.084
0.075
0.075
0.075
0.075
0.085
0.11
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
LEAD
(ug)
0
0
2.5
0.5
2.5 <
0.5
ZINC
(ug)
0.34
0.50
0.45
0.48
0.88
0.54
0.50
2.12
0.98
0.63
0.71
1.08
0.62
0.81
0.71
0.94
0.78
0.51
0.66
0.68
3.14
0.74
0.88
0.58
1.44
7.53
0.63
1.77
0.39
0.38
0.81
0.42
0.36
0.33
0.41
0.32
0.36
ZINC
(ug)
85.6
53.9
5.6
14
1.25
66
STRONTIUM
(ug)
0.72
1.23
1.58
10.23
27.44
1.64
9.86
38.86
21.02
44.90
87.57
147.92
82.74
30.76
99.00
173.30
158.90
91.50
33.16
80.82
91.05
111.80
122.56
8.72
74.46
101.06
91.47
206.86
8.16
< 0.30 <
< 0.30 <
< 0.30 <
< 0.30 <
? 0.30 <
0.36
0.33 7
< 0.30 <
STRONTIUM
(ug)
13.13
10.75
8.4
3.8
0.93
< 0.2
CHROMIUM
(ug)
0.57
0.84
1.05
6.44
17.02
1.10
6.03
23.37
12.75
25.78
51.41
87.64
48.74
17.88
59.48
102.72
94.56
55.22
19.91
45.36
51.96
64.04
68.46
5.07
41.82
56.86
50.81
118.34
4.82
0.30
0.30
0.30
0.30
0.30
0.32
0.28
0.30
CHROMIUM
(ug)
30.08
40.6
5.4
6.40
1.28
17.00
AVG FLOU LEAD
(L/NIN)
3.030
3.033
3.098
3.050
2.992
3.014
3.014
3.026
3.067
3.021
2.996
3.079
3.053
3.061
3.064
3.058
3.028
3.056
3.054
3.018
3.042
3.101
3.048
3.017
3.017
3.054
3.130
2.979
3.039
2.999
3.057
2.993
2.977
3.054
2.993
3.010
3.000
SAMPLE
(N3)
.109
.156
.109
.109
.109
.109
(ug/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
< MDL
0.4
0.4
< MDL
< MDL
< MDL
< MDL
< MDL
0.4
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
0.4
< MDL
< MDL
< MDL
< MDL
0.4
0.6
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< 0.4
LEAD
(UB/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
ZINC
(ug/M3)
1.7
2.5
2.3
2.4
4.5
2.8
2.5
10.6
4.8
3.2
3.6
5.3
3.1
4.0
3.5
4.6
3.9
2.5
3.3
3.4
15.6
3.6
4.4
2.9
7.2
37.4
3.0
9.1
2.0
1.9
4.1
2.2
120.9
1.7
2.1
1.6
1.8
ZINC
(ug/M3)
77.2
46.6
5.0
12.6
< MDL
59.5
STRONTIUM
(ug/M3)
3.6
6.1
8.0
50.8
139.0
8.4
49.6
194.6
103.9
225.2
442.9
727.9
410.7
152.3
482.3
846.0
795.1
453.7
164.5
405.7
453.5
546.3
609.2
43.8
374.0
501.4
442.8
1068.5
41.3
< MDL
< MDL
< MDL
< MDL
< MDL
1.9
1.7
< 1.5
STRONTIUM
(ug/M3)
11.8
9.3
7.6
3.4
0.8
0.0
CHROMIUM
(ug/M3)
2.9
4.2
5.3
32.0
86.2
5.6
30.3
117.0
63.0
129.3
260.0
431.3
241.9
88.5
289.8
501.4
473.2
273.8
98.8
227.7
258.8
313.0
340.3
25.5
210.1
282.1
246.0
611.3
24.4
< MDL
< MDL
< MDL
< MDL
< MDL
1.6
< MDL
< 1.5
CHROMIUM
(ug/M3)
27.1
35.1
4.9
5.8
1.2
15.3
-------
TEST: METALS *2
DATE: 06-24-92 PM
METHOD: NIOSH 7300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT: LT GREEN PRIMER
OBJECT: SPLITTERS
D E INITIALS:
0 A INITIALS:
ACUREX BASE
GRID LOC SAMPLE f SAMPLE * PUMP *
PRE-CAL POST-CAL RUN TIME
(nl/min) (ml/min) (min)
LEAD
(ug)
ZINC
(ug)
STRONTIUM
(ug)
CHROMIUM AVG FLOU LEAD
(ug) (L/MIH) (ug/M3)
ZINC STRONTIUM CHROMIUM
(ug/M3) (ug/M3) (ug/M3)
RECIRC ACETONE EX921386 < 2.5 10.9 4.2 4.9 1.156
NITRIC EX921387 < 0.5 20 5.7 18.00 1.156
FILTER EX921416 < 2.5 < 1.25 0.85 1.7 1.156
IMPINGER EX921417 < 0.5 23 < 0.2 16.00 1.156
MDL
MDL
MDL
MDL
9.4
17.3
MDL
19.9
3.6
4.9
0.7
0.0
4.2
15.6
1.5
13.8
-------
TES
DAI
HETHC
GRID C
T: METALS #2
E: 06-24-92 PN
»: NIOSH 7300
HART 1 - LEAD
Painter Over
0.6
Painter Under
< HDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
** < MDL 1NIN
TRAVIS AFB D E INITIALS:
PAINT BOOTH TESTS 0 A INITIALS:
ACUREX PROJECT 8485
EXHAUST GRID
1234
< MDL < MDL < MDL < MDL
< MDL
5678
< MDL < MDL 0.4 0.4
9 10 11 12
< MDL < MDL < MDL < MDL
21 22 23 24
< MDL 0.4 < MDL < MDL
< MDL
13 14 15 16
< MDL < MDL 0.4 < MDL
< MDL
»
17 18 19 20
< HDL < MDL < MDL 0.4
0
0
FIELD BLANK
< 0.4
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: SPLITTERS OSHA TWA: 50 ug/M3
GRID MDL: 0.075 ug/SANPLE
PAINTER MDL: 0.075 ug/SANPLE
EXHAUST DUCT: < HDL
RECIRC DUCT: < MDL
-------
TES
DAI
MEW
GRID C
!T: METALS #2
E: 06-24-92 PM
»: NIOSH 7300
HART 2 - ZINC
Painter Over
9.1
Painter Under
2.0
INLET GRID A
1A
1.9
2A
4.1
3A
2.2
** 120.9 1NIN
TRAVIS AFB 0 E INITIALS:
PAINT BOOTH TESTS 0 A INITIALS:
ACUREX PROJECT 8485
EXHAUST GRID
•
1234
1.7 2.5 2.4 4.5
2.3
5 6 7 8
2.8 2.5 10.6 4.8
9 10 11 12
3.2 3.6 5.3 3.1
21 22 23 24
4.0 3.5 4.6 2.5
3.9
13 14 15 16
3.3 3.4 3.6 4.4
15.6
17 18 19 20
2.9 7.2 37.4 3.0
0
0
FIELD BLANK
1.8
INLET GRID B
IB
1.7
2B
2.1
3B
1.6
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: SPLITTERS OSHA TWA: 1000 ug/M3
GRID MDL: 0.3 ug/SANPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 77.2
RECIRC DUCT: 46.6
-------
TES
DAI
METHC
GRID C
T: METALS 92
E: 06-24-93 PM
D: NIOSH 7300
HART 3 - STRONTIUM
Painter Over
1068.5
Painter Under
41.3
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
** < MDL 1MIM
TRAVIS AFB D E INITIALS:
PAINT BOOTH TESTS 0 A INITIALS:
ACUREX PROJECT 8485
EXHAUST GRID
1234
3.6 6.1 50.8 139.0
8.0
5 6 7 8
8.4 49.6 194.6 103.9
9 10 11 12
225.2 442.9 727.9 410.7
21 22 23 24
152.3 482.3 846.0 453.7
795.1
13 14 15 16
164.5 405.7 546.3 609.2
453.5
17 18 19 20
43.8 374.0 501.4 442.8
0
0
FIELD BLANK
< 1.5
INLET GRID B
IB
< MDL
2B
1.9
3B
1.7
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: SPLITTERS OSHA TWA: 77 ug/M3
GRID MDL: 0.3 ug/SAMPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 11.8
RECIRC DUCT: 9.3
-------
TEST: METALS »2 TRAVIS AFB D E INITIALS: 0
DATE: 06-24-92 PM PAINT BOOTH TESTS 0 A INITIALS: 0
METHOD: NIOSH 7300 ACUREX PROJECT 8485
GRID CHART 4 - CHROMIUM
Painter Over
611.3
Painter Under
24.4
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
** < HDL 1NIN
EXHAUST GRID
1234
2.9 4.2 32.0 86.2
5.3
5678
5.6 30.3 117.0 63.0
9 10 11 12
129.3 260.0 431.3 241.9
21 22 23 24
68.5 289.8 501.4 273.8
473.2
13 14 15 16
98.8 227.7 313.0 340.3
258.8
17 18 19 20
25.5 210.1 282.1 246.0
PAINT TTPE: LT GREEN PRIMER UNITS: ug/W GRID HDL: 0.3 ug/SAMPLE
EXHAUST D
FIELD BLANK
< 1.5
INLET GRID B
IB
< MDL
2B
1.6
3B
< HDL
UCT: 27.1
OBJECT: SPLITTERS OSHA TWA: 50 UQ/M3 PAINTER MDL: 0.3 ug/SAMPLE RECIRC DUCT: 35.1
-------
TEST: METALS #3
DATE: 06-25-92 AMI
HETHQO: NIOSH 7300
ACUREX BASE
GRID LOG SAMPLE * SAMPLE *
1
2
3
4
5
6
7
7 OUP
8
9
10
11
12
21
22
23
24
24 OUP
13
13 OUP
U
15
16
17
18
19
20
f over
P under
1A
2A
2A OUP
3A
IB
2B
3B
F BLANK
LOCATION
EXHAUST
RECIRC
68 EX921208
61 EX921209
87 EX921210
112 EX921211
105 EX921212
71 EX921213
62 EX9212U
117 EX921215
76 EX921216
74 EX921217
130 EX921218
55 EX921219
96 EX921220
100 EX921221
53 EX921222
119 EX921223
65 EX921224
73 EX92122S
52 EX921226
124 EX921227
64 EX921228
75 EX921229
97 EX921230
115 EX921231
57 EX921232
109 EX921233
80 EX921234
59 EX921269
66 EX921270
67 EX921201
56 EX921202
101 EX921203
58 EX921204
60 EX921205
106 EX921206
116 EX921207
72 6X921278
SAMPLES
ACETONE
EX92138B
EX921392
PUMP *
25
10
13
23
22
40
17
28
16
41
24
43
32
7
18
42
5
14
20
8
1
31
21
11
34
15
29
30
35
33
27
6
3
19
12
4
26
NITRIC
EX921389
EX921393
TRAVIS AFB PAINT: LT GREEN PRIMER
PAINT BOOTH TESTS OBJECT: BRAKE PARTS. HUBS. RAMP
ACUREX PROJECT 8485
PRE-CAL POST-CAL RUN TIME LEAD ZINC STRONTIUM CHROMIUM
(ml/min) (ml/min) (min)
2981 2968 58
3000 2980 59
3033 3010 56
2977 3006 58
2997 3030 50
2991 3024 58 <
3048 3015 58 <
3030 3027 58
2991 2994 58
2977 2906 58
3018 3015 58
3082 3048 58
3088 3057 58
2994 2951 58
3057 3036 58 <
3024 3042 58 <
2962 2950 59 <
3066 3039 58 <
3036 3035 58 <
3075 3042 59 <
2991 3003 59
3018 2991 58 <
3024 3007 58 <
2980 2977 59 <
3054 3021 58
2997 2985 58
2988 2928 58 <
3030 2940 57
3060 2928 56 <
3082 3021 57
3051 3006 57
3006 3033 57
3012 2977 57
3072 3012 57
3012 2974 55
3015 2940 56
58
SAMPLE
FILTER IMPINGER (CU FT)
EX921390 EX921391 38.00
EX921348 EX921349 37.31
EXHAUST ACETONE EX921388 <
NITRIC EX921389 <
FILTER EX921390 <
IMPINGER EX921391 <
(ug)
1.610
0.660
2.100
3.720
0.077
0.075
0.075
0.091
0.130
0.110
0.083
0.200
0.076
0.082
0.075
0.075
0.075
0.075
0.075
0.075
0.210
0.075
0.075
0.075
0.090
0.093
0.075
0.100
0.075
20.460
0.680
0.250
0.770
1.880
2.600
2.880
0.330
LEAD
(ug)
0
14.5
2.5
0.5
2.5 <
0.5
(ug)
3.99
2.56
25.78
4.32
3.87
1.65
1.92
1.65
4.06
5.88
30.80
2.79
1.38
1.95
1.89
1.44
2.44
15.62
1.36
2.82
4.80
3.03
7.32
5.60
4.69
5.60
3.71
3.32
2.44
6.18
1.95
0.88
2.88
5.91
4.71
4.98
1.98
ZINC
(ug)
12.3
120.5
5.5
4.1
1.25
2.7
(ug)
1.61
0.99 <
2.16
2.46
2.54
3.57
5.73
4.89
4.38
11.30
30.98
26.64
12.36
16.97
45.71
25.71
12.56
18.03
24.39
24.50
48.99
26.12
26.88
19.68
40.80
69.80
19.77
19.18
< 0.30
< 0.75
< 0.75 <
< 0.75 <
< 0.75 <
< 0.75 <
< 0.75 <
< 0.75 <
0.32 <
STRONTIUM
(ug)
5.9
5.7
5.1
0.8
< 0.5
< 0.2
(ug)
1.32
0.75
1.84
2.64
1.77
5.64
5.01
3.00
2.74
7.32
23.51
15.90
8.25
13.20
27.36
15.27
7.48
10.65
14.72
14.62
29.34
15.93
16.17
11.54
24.50
41.68
11.96
11.56
1.14
4.35
0.75
0.75
0.75
0.75
0.75
0.75
0.75
CHROMIUM
(ug)
8.55
88.7
3.8
2.4
0.95
1.4
D E INITIALS:
0 A INITIALS:
AVG FLOW LEAD
(L/MIN)
2.975
2.990
3.022
2.992
3.014
3.008
3.032
3.029
2.993
2.942
3.017
3.065
3.073
2.973
3.047
3.033
2.956
3.053
3.036
3.059
2.997
3.005
3.016
2.979
3.038
2.991
2.958
2.985
2.994
3.052
3.029
3.020
2.995
3.042
2.993
2.978
3.000
SAMPLE
(N3)
1.075
1.056
1.075
1.075
1.075
1.075
(ug/M3)
9.3
3.7
12.4
21.4
0.5
< MDL
< MDL
0.5
0.7
0.6
0.5
1.1
0.4
0.5
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
1.2
< HDL
< MDL
< MDL
0.5
0.5
< MDL
0.6
< MDL
117.6
3.9
1.5
4.5
10.8
15.8
17.3
1.9
LEAD
(ug/M3)
< MDL
13.7
< MDL
< MDL
< MDL
< MDL
LJL
ZINC
(ug/M3)
23.1
14.5
152.4
24.9
25.7
9.5
10.9
9.4
23.4
34.5
176.0
15.7
7.7
11.3
10.7
8.2
14.0
88.2
7.7
15.6
27.1
17.4
41.9
31.9
27.8
32.3
21.6
19.5
14.6
35.5
11.3
5.1
16.9
34.1
28.6
29.9
11.4
ZINC
(ug/M3)
11.4
114.1
5.1
3.8
< MDL
2.5
STRONTIUM
(ug/M3)
9.3
5.6
12.8
14.2
16.9
20.5
32.6
27.8
25.2
66.2
177.1
149.9
69.4
98.4
258.7
146.2
72.0
101.8
138.5
135.8
277.1
149.9
153.7
112.0
231.6
402.4
115.2
112.7
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
1.8
STRONTIUM
(ug/M3)
5.5
5.4
4.7
0.7
< MDL
< MDL
CHROMIUM
(ug/M3)
7.7
< MDL
10.9
15.2
11.7
32.3
28.5
17.1
15.8
42.9
134.4
89.4
46.3
76.6
154.8
86.8
42.9
60.2
83.6
81.0
165.9
91.4
92.5
65.7
139.1
240.3
69.7
67.9
6.8
25.0
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< 4.3
CHROMIUM
(ug/M3)
8.0
84.0
3.5
2.2
0.9
1.3
-------
TEST: METALS *3
DATE: 06-25-92 AMI
METHOD: NIOSH 7300
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT:
OBJECT:
LT GREEN PRIMER
BRAKE PARTS. HUBS. RAMP
D E INITIALS:
0 A INITIALS:
LJL
ACUREX BASE
GRID LOC SAMPLE ff SAMPLE f PUMP *
PRE-CAL POST-CAL RUN TIME
(nl/min) (ml/min) (min)
LEAD
(ug)
ZINC
(ug)
STRONTIUM
(ug)
CHROMIUM AVG FLOW LEAD
(ug) (L/MIN) (ug/M3)
ZINC STRONTIUM CHROMIUM
(ug/M3) (ug/M3) (ug/M3)
RECIRC ACETONE EX921392 < 25 25 2.4 3 1.056
NITRIC EX921393 12 34 3.3 72 1.056
FILTER EX921348 < 2.5 3.5 < 0.5 13.7 1.056
IMPINGER EX921349 < 0.5 58 < 0.2 < 0.2 1.056
MDL
11.4
MDL
MDL
23.7
32.2
3.3
54.9
2.3
3.1
MDL
MDL
2.8
68.2
13.0
< MDL
CO
-------
TEST: METALS *3
DATE: 06-25-92 AM1
METHOD: MIOSH 7300
GRID CHART 1 - LEAD
TRAVIS AF8
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
Q A INITIALS: 0
CO
IN)
Painter Over
0.6
Painter Under
< MOL
INLET GRID A
1A
117.6
2A
3.9
1.5
3A
4.5
EXHAUST GRID
1 2 3 4
9.3 3.7 12.4 21.4
5678
0.5 < MDL < MDL 0.7
0.5
9 10 11 12
0.6 0.5 1.1 0.4
21 22 23 24
0.5 < HDL < MDL < MDL
< MDL
13 14 15 16
< MDL 1.2 < MDL < MDL
< MDL
17 18 19 20
< MDL 0.5 0.5 < MDL
Field Blank
1.9
INLET GRID B
IB
10.8
2B
15.8
3B
17.3
PAINT TYPE: LT GREEN PRIMER UNITS: ug/W GRID MDL: 0.075 ug/SAMPLE
OBJECT: BRAKE PARTS, NUBS, RAMP OSHA TUA: 50 ug/M3 PAINTER MDL: 0.075 ug/SAMPLE
EXHAUST DUCT: < MDL
RECIRC DUCT: 13.7
-------
TEST: METALS «
DATE: 06-25-92 AMI
METHOD: NIOSH 7300
GRID CHART 2 - ZINC
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
19.5
Painter Under
U.6
INLET GRID A
1A
35.5
2A
11.3
5.1
3A
16.9
EXHAUST GRID
1234
23.1 14.5 152.4 24.9
5678
25.7 9.5 10.9 23.4
9.4
9 10 11 12
34.5 176.0 15.7 7.7
21 22 23 24
11.3 10.7 8.2 14.0
88.2
13 14 15 16
7.7 27.1 17.4 41.9
15.6
t
17 18 19 20
31.9 27.8 32.3 21.6
Field Blank
11.4
INLET GRID B
IB
34.1
2B
28.6
3B
29.9
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3 GRID HDL: 0.3 ug/SANPLE
OBJECT: BRAKE PARTS. HUBS, RAMP OSHA TWA: 1000 ug/ PAINTER HDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 11.4
RECIRC DUCT: 114.1
-------
TEST: METALS *3
DATE: 06-25-92 AMI
METHOD: NIOSH 7300
GRID CHART 3 - STRONTIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
0 E INITIALS: LJL
0 A INITIALS: 0
Painter Over
112.7
Painter Under
< MOL
INLET GRID A
1A
< MOL
2A
< MDL
< HDL
3A
< MDL
PAINT TYPE: LT Gl
OBJECT: BRAN
iEEN PRIMI
E PARTS, 1
EXHAUST GRID
1234
9.3 5.6 12.8 14.2
16.9 20.5 32.6 25.2
27.8
9 10 11 12
66.2 177.1 149.9 69.4
21 22 23 24
98.4 258.7 146.2 72.0
101.8
13 14 15 16
138.5 277.1 149.9 153.7
135.8
17 18 19 20
112.0 231.6 402.4 115.2
•R UNITS: ug/W GRID MDL: 0.3 ug/SAMPLE
•JBS.OSHA TUA: 77 ug/M3 PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST 1
RECIRC I
Field Blank
1.8
INLET GRID B
IB
< MDL
28
< MDL
38
< MDL
•UCT: 5.5
UCT: 5.4
-------
TEST: METALS #3
DATE: 06-25-92 AMI
METHOD: NIOSH 7300
GRID CHART 4 - CHROMIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
67.9
Painter Under
6.8
INLET GRID A
1A
25.0
2A
< MDL
< MDL
3A
< MDL
PAINT TTPE: LT Gf
OBJECT: BRAKI
IEEN PRIME
: PARTS. 1
EXHAUST GRID
1234
7.7 < MDL 10.9 15.2
5678
11.7 32.3 28.5 15.8
17.1
9 10 11 12
42.9 134.4 89.4 46.3
21 22 23 24
76.6 154.8 86.8 42.9
60.2
13 14 15 16
83.6 165.9 91.4 92.5
81.0
17 18 19 20
65.7 139.1 240.3 69.7
:R UNITS: ug/W GRID MDL: 0.3 ug/SAMPLE
•JBS.OSNA TWA: 50 ug/M3 PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST 0
RECIRC 0
Field Blank
< 4.3
INLET GRID B
IB
< MDL
28
< MDL
3B
< MDL
UCT: 8.0
lUCT: 84.0
-------
TEST: METALS «4
DATE: 06-26-92 AMI
METHOD: NIOSH 7300
ACUREX BASE
GRID LOG SAMPLE * SAMPLE *
1
2
3
4
5
6
6 DUP
7
a
9
10
11
11 DUP
12
21
22
23
24
13
K
15
16
17
18
18 DUP
19
20
P over
P under
1A
2A
3A
1B
2B
38
F BLANK
144 EX921242
125 EX921243
122 EX921244
205 EX921245
98 EX921246
110 EX921247
51 EX921253
141 EX921248
85 EX921249
139 EX921250
84 EX921251
102 EX921252
63 EX921254
145 EX9212S5
81 EX921265
142 EX921266
151 EX921267
153 EX921268
159 EX921256
147 EX921257
133 EX921258
86 EX921259
192 EX921260
149 EX921261
143 EX921262
200 EX921263
114 EX921264
111 EX921276
82 EX921277
70 EX921236
123 EX921237
54 EX921238
148 EX921239
127 EX921240
166 EX921241
158 EX921235
PUMP *
13
28
29
50
15
19
24
33
46
6
42
21
12
48
4
31
35
53
11
30
32
55
1
18
14
49
45
34
40
52
54
51
20
17
43
7
TRAVIS AFB PAINT: LT GREEN PRIMER
PAINT BOOTH TESTS OBJECT: THRUST REVERSER
ACUREX PROJECT 8485
PRE-CAL POST -C At RUN TIME LEAD ZINC STRONTIUM
(ml/min) (ml/min) (min)
2971 2903 77 <
3029 3012 80 <
3063 3057 80 <
3033 3079 81 <
2988 3003 79 <
3045 2994 79 <
2988 3018 81 <
3027 3051 81 <
3030 3063 81 <
3018 3063 78 <
3033 3024 80
3039 3012 80
2994 3003 81
2997 3107 80
3045 2977 78 <
2988 2965 80
3057 3066 80
3015 3091 80
3024 3027 79
3033 2971 78
3024 2928 81
2978 3015 80
3036 2951 79 <
3024 3018 78
3003 3003 81 <
3048 3072 80
3009 3018 81
3048 3003 77
2971 2945 77 <
3018 3066 77 <
3021 3045 77 <
2985 3000 77 <
2965 2985 76 <
3015 3009 76
3012 3012 76 <
79 <
(ug)
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.100
0.110
0.11
0.095
0.075
0.09
0.12
0.11 <
0.1
0.078 <
0.19
0.095
0.075
0.077
0.075
0.098
0.17
0.098
0.075
0.075
0.075
0.075
0.075
0.1
0.075
0.075
(ug)
0.48
1.04
0.84
1.02
1.17
1.10
1.08
0.52
0.80
0.42
2.08
0.52
0.62
0.50
0.48
0.51
0.57
0.30
3.32
0.30
1.82
0.38
0.69
0.66
0.42
1.10
1.22
0.38
0.39
5.42
1.23
2.74
0.78
4.12
1.08
3.58
(ug)
1.11
4.71
28.48
45.36
7.38
31.25
17.43
83.54
71.88
39.45
93.64
167.79
175.76
134.55
5.18
122.61
201.46
180.76
19.18
119.78
204.99
145.74
6.69
45.44
47.67
107.84
114.36
157.58
15.87
0.64
0.38
0.32
* 0.52
0.51
0.52
< 0.30 <
CHROMIUM
(ug)
0.71
2.90
16.83
26.64
4.46
21.71
10.42
49.76
43.59
22.78
54.88
96.84
106.70
77.82
29.94
71.22
114.36
104.70
11.56
69.06
117.51
85.04
4.06
26.90
27.72
62.74
66.21
91.44
9.50
0.54
0.42
0.30
0.51
0.44
0.42
0.30
D E INITIALS:
0 A INITIALS:
AVG FLOW LEAD
(L/MIN) (ug/M3)
2.937 < MDL
3.021 < MDL
3.060 < MDL
3.056 < MDL
2.996 < MDL
3.020 < MDL
3.003 < MDL
3.039 < MDL
3.047 < MDL
3.041 < MDL
3.029 0.4
3.026 0.5
2.999 0.5
3.052 0.4
3.011 < MDL
2.977 0.4
3.062 0.5
3.053 0.5
3.026 0.4
3.002 0.3
2.976 0.8
2.997 0.4
2.994 < HDL
3.021 0.3
3.003 < MDL
3.060 0.4
3.014 0.7
3.026 0.4
2.958 < MDL
3.042 < MDL
3.033 < MDL
2.993 < MDL
2.975 < MDL
3.012 0.4
3.012 < MDL
3.000 < 0.3
BN & LJL
ZINC
(ug/M3)
2.1
4.3
3.4
4.1
4.9
4.6
4.4
2.1
3.2
1.8
8.6
2.1
2.6
2.0
2.0
2.1
2.3
< MDL
13.9
< MDL
7.6
1.6
2.9
2.8
1.7
4.5
5.0
1.6
1.7
23.1
5.3
11.9
3.4
18.0
4.7
15.1
STRONTIUM
(ug/M3)
4.9
19.5
116.3
183.2
31.2
131.0
71.7
339.4
291.3
166.3
386.5
693.2
723.7
551.1
22.1
514.9
822.6
740.1
80.2
511.5
850.4
608.0
28.3
192.8
196.0
440.5
468.5
676.4
69.7
2.7
1.6
1.4
2.3
2.2
2.3
< 1.3
CHROMIUM
(ug/M3)
3.1
12.0
68.7
107.6
18.8
91.0
42.8
202.1
176.6
96.1
226.5
400.1
439.3
318.7
127.5
299.1
466.9
428.7
48.4
294.9
487.5
354.7
17.2
114.2
114.0
256.3
271.2
392.5
41.7
2.3
1.8
1.3
2.3
1.9
1.8
< 1.3
0.000 no •anpleno sampleno SMpleno ample
LOCATION
EXHAUST
REC1RC
SAMPLES
ACETONE
EX921447
EX92145S
NITRIC
EX921448
EX921456
SAMPLE
FILTER INPINGER (CU FT)
EX921449 EX921450 48.30
EX9214S7 EX921458 46.09
EXHAUST ACETONE EX921447 <
NITRIC EX921448 <
FILTER EX921449 <
1MPINGER EX921450 <
LEAD
(ug)
0
0
2.5
0.5
2.5 <
0.5
ZINC
(ug)
25.5
56
5.2
2.3
1.25
18
STRONTIUM
(ug)
16.8
14.08
10.6
4.6
1.6
< 0.2
CHROMIUM
(ug)
21.58
43
6.8
3.50
1.88
9.40
SAMPLE LEAD
(N3) (ug/M3)
.367 < MDL
.304 < MDL
.367 < MDL
.367 < MDL
.367 < MDL
.367 < MDL
ZINC
(ug/M3)
18.7
42.9
3.8
1.7
< MDL
13.2
STRONTIUM
(ug/M3)
12.3
10.8
7.8
3.4
1.2
< MDL
CHROMIUM
(ug/M3)
15.8
33.0
5.0
2.6
1.4
6.9
-------
TEST: METALS *4 TRAVIS AFB PAINT: LT GREEN PRIMER 0 E INITIALS: BN I LJL
DATE: 06-26-92 AMI PAINT BOOTH TESTS OBJECT: THRUST REVERSER Q A INITIALS:
METHOD: NIOSH 7300 ACUREX PROJECT 8465
ACUREX BASE PRE-CAL POST-CAL RUN TIME LEAD ZINC STRONTIUM CHROMIUM AVG FLOW LEAD ZINC STRONTIUM CHROMIUM
GRID LOG SAMPLE * SAMPLE * PUMP * (ml/min) (ml/min) (min) (ug) (ug) (ug) (ug) (L/MIN) (ug/M3) (ug/M3) (ug/M3) (ug/M3)
RECIRC ACETONE EX92H55 < 2.5 11 3.7 3.6 1.304 < MDL 8.4 2.8 2.8
NITRIC EX921456 < 0.5 25 9.6 26.00 1.304 < MDL 19.2 7.4 19.9
FILTER EX921457 < 2.5 < 1.25 0.78 1.4 1.304 < MDL < MDL 0.6 1.1
IMPINGER EX921458 < 0.5 20 < 0.2 12.00 1.304 < MDL 15.3 < MDL 9.2
CO
-------
TEST: METALS «4
DATE: 06-26-92 AMI
METHOD: NIOSH 7300
GRID CHART 1 - LEAD
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: BN ft LJL
0 A INITIALS: 0
Painter Over
0.4
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
< MDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< MDL 0.4 0.5 0.4
0.5
21 22 23 24
< MDL 0.4 0.5 0.5
13 14 15 16
0.4 0.3 0.8 0.4
17 18 19 20
< MDL 0.3 0.4 0.7
< MDL
Field Blank
< 0.3
INLET GRID B
IB
< MDL
2B
0.4
3B
< MDL
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: THRUST REVERSER OSHA TWA: 50 ug/M3
GRID MDL: 0.075 ug/SAMPLE EXHAUST DUCT: < MDL
PAINTER MDL: 0.075 ug/SAMPLE RECIRC DUCT: < MDL
-------
TEST: METALS *4
DATE: 06-26-92 AMI
METHOD: NIOSH 7300
GRID CHART 2 - ZINC
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: BN & LJL
0 A INITIALS: 0
Painter Over
1.6
Painter Under
1.7
INLET GRID A
1A
23.1
2A
5.3
3A
11.9
EXHAUST GRID
1234
2.1 4.3 3.4 4.1
5 A 7 ft
4.9 4.6 2.1 3.2
4.4
9 10 11 12
1.8 8.6 2.1 2.0
2.6
21 22 23 24
2.0 2.1 2.3 < MDL
13 14 15 16
13.9 < MDL 7.6 1.6
,
17 IB 19 20
2.9 2.8 4.5 5.0
1.7
Field Blank
15.1
INLET GRID B
IB
3.4
2B
18.0
3B
4.7
PAINT TYPE: LT GREEN PRIMER UNITS: ug/N3
OBJECT: THRUST REVERSER OSHA TWA: 1000 ug/M3
GRID MDL: 0.3 ug/SAMPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 18.7
RECIRC DUCT: 42.9
-------
TEST: METALS #4
DATE: 06-26-92 AMI
METHOD: N10SH 7300
GRID CHART 3 - STRONTIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: BN & LJL
0 A INITIALS: 0
Painter Over
676.4
Painter Under
69.7
INLET GRID A
1A
2.7
2A
1.6
3A
1.4
EXHAUST GRID
1234
4.9 19.5 116.3 183.2
5678
31.2 131.0 339.4 . 291.3
71.7
9 10 11 12
166.3 386.5 693.2 551.1
723.7
21 22 23 24
22.1 514.9 822.6 740.1
13 14 15 16
80.2 511.5 850.4 608.0
17 18 19 20
28.3 192.8 440.5 468.5
196.0
Field Blank
< 1.3
INLET GRID B
IB
2.3
2B
2.2
3B
2.3
PAINT TYPE: LT GREEN PRIMER UNITS: ug/M3
OBJECT: THRUST REVERSER OSHA TWA: 7? UQ/M3
GRID HDL: 0.3 ug/SANPLE
PAINTER HDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 12.3
RECIRC DUCT: 10.8
-------
TEST: METALS «4
DATE: 06-26-92 AM1
METHOD: MIOSH 7300
GRID CHART 4 - CHROMIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
0 E INITIALS: BN & LJL
0 A INITIALS: 0
Painter Over
392.5
Painter Under
41.7
INLET GRID A
1A
2.3
2A
1.8
3A
1.3
EXHAUST GRID
1234
3.1 12.0 68.7 107.6
5678
18.8 91.0 202.1 176.6
42.8
9 10 11 12
96.1 226.5 400.1 318.7
439.3
21 22 23 24
127.5 299.1 466.9 428.7
13 14 15 16
48.4 294.9 487.5 354.7
*
17 18 19 20
17.2 114.2 256.3 271.2
114.0
Field Blank
< 1.3
INLET GRID B
1B
2.3
2B
1.9
3B
1.8
PAINT TTPE: LT GREEN PRIMER UNITS: ug/W
OBJECT: THRUST REVERSER OSHA TWA: 50 ug/M3
GRID MDL: 0.3 ug/SAMPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 15.8
RECIRC DUCT: 33.0
-------
TEST: METALS *5
DATE: 06-26-92 AM2
METHOD: N10SH 7300
Non paint time deducted
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
PAINT:
OBJECT:
GUNSHIP GRAY POLY
THRUST REVERSER
D E INITIALS:
0 A INITIALS:
LJL
IO
ACUREX BASE PRE-CAL POST-CAL RUN TIME
GRID LCC SAMPLE * SAMPLE * PUMP * (ml/min) (ml/min) (min)
1
2
3
4
5
6
6 DUP
7
8
9
10
11
12
21
22
23
24
13
14
15
16
17
18
19
20
20 DUP
P over
P under
1A
2A
3A
1B
2B
3B
BLANK
189 EX921137
157 EX921138
188 EX921139
198 EX921140
211 EX921141
206 EX921142
182 EX921143
177 EX921144
210 EX921145
204 EX921146
136 EX921147
197 EX921148
135 EX921149
194 EX921150
181 EX921151
126 EX921152
134 EX921153
172 EX921154
195 EX921155
203 EX921156
128 EX921157
167 EX92115B
171 EX921159
185 EX921160
138 EX921161
178 EX921162
168 EX921163
176 EX921164
191 EX921131
186 EX921132
215 EX921133
154 EX921134
152 EX921135
187 EX921136
12
48
17
6
28
42
45
43
4
21
46
54
20
29
19
55
11
32
31
50
13
33
53
52
18
14
34
40
15
1
24
35
49
30
3003
3033
3009
3063
3012
3024
3018
3012
2977
3012
3063
3045
2985
3057
2994
3015
3027
3012
2965
3045
2983
3051
3036
3066
3018
3003
3003
2945
3003
2951
3018
3066
3039
2971
3060
3039
3006
2988
3015
3042
3042
2985
2991
3021
3066
3069
2991
3027
3006
3009
3042
3060
3000
3036
3012
3060
3057
3091
3012
2994
3015
2940
3024
3006
3048
3060
3051
2983
66 <
66 <
66 <
67 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
66 <
68 <
66 <
66 <
66 <
65 <
66 <
66 <
66 <
67 <
67 <
54 <
66 <
67 <
67 <
66
66 <
66 <
66 <
LEAD
(ug)
0.075
0.075
0.075
0.075
0.075
0.075 <
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.075
0.088
0.075
0.075
0.075
ZINC STRONTIUM CHROMIUM
(ug) (ug) (ug)
0.92 <
0.34 <
0.30 <
0.34 <
0.46 <
0.30 <
0.48 <
4.50 <
0.34 <
0.54 <
0.62 <
7.05 <
8.42 <
0.38 <
0.48 <
0.76 <
0.34 <
0.30 <
0.57 <
0.33 <
0.54 <
0.69 <
0.57 <
2.18 <
0.66 <
0.68 <
0.52
0.56 <
0.41 <
5.78 <
3.68 <
0.78 <
0.78 <
0.42 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30 <
0.30
0.30
0.30
0.30 <
0.30
0.30 <
0.30
0.81
0.30 <
0.30 <
0.30 <
0.30 <
0.30 7
0.30 <
0.30 <
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.30
0.21
0.30
0.30
0.30
0.30
0.30
0.30
0.36
0.41
0.56
0.30
0.34
0.30
0.30
0.57
0.30
0.30
0.30
0.30
0.09
0.30
0.30
AVG FLOW LEAD ZINC STRONTIUM
(L/MIN) (ug/M3) (ug/M3) (ug/H3)
3.032
3.036
3.008
3.026
3.014
3.033
3.030
2.999
2.984
3.017
3.065
3.057
2.988
3.042
3.000
3.012
3.035
3.036
2.983
3.041
2.998
3.056
3.047
3.079
3.015
2.999
3.009
2.943
3.014
2.979
3.033
3.063
3.045
2.977
0.000
0.000
0.000
< MDL 4.6 < HDL
< MDL 1.7 < MDL
< MDL 1.5 < MDL
< MDL 1.7 < MDL
< HDL 2.3 < HDL
< MDL < HDL < MDL
< HDL 2.4 < MDL
< HDL 22.7 < HDL
< HDL 1.7 < MDL
< MDL 2.7 < MDL
< MDL 3.1 < MDL
< MDL 34.9 < HDL
< HDL 42.7 < MDL
< HDL 1.9 < HDL
< HDL 2.4 < HDL
< HDL 3.8 < MDL
< HDL 1.6 < HDL
< HDL 1.5 < HDL
< MDL 2.9 < HDL
< HDL 1.6 < HDL
< MDL 2.8 < MDL
< MDL 3.4 < HDL
< HDL 2.8 < MDL
< MDL 10.7 < MDL
< MDL 3.3 < HDL
< HDL 3.4 < HDL
< HDL 3.2 5.0
< HDL 2.9 < MDL
< NDL 2.0 < HDL
< HDL 29.0 < HDL
0.4 18.4 < HDL
< HDL 3.9 < HDL
< HDL 3.9 < HDL
< HDL 2.1 < HDL
CHROMIUM
(ug/M3)
< MDL
< MDL
< MOL
< MDL
< NDL
MDL
MDL
HDL
HDL
HDL
< HDL
< MDL
1.1
< HDL
< NDL
< NDL
< NDL
< HDL
< HDL
1.8
2.1
2.8
< HDL
1.7
< HDL
1.5
3.5
< NDL
< HDL
< HDL
< HDL
< HDL
< NDL
< HDL
no sampleno sampleno sampleno sample
no sampleno sampleno sampleno sample
no sampleno sampleno sampleno sample
LOCATION
EXHAUST
RECIRC
SAMPLES
ACETONE NITRIC FILTER IMPINGER
EX921451 EX921452 EX921453 EX921454
EX921459 EX921460 EX921461 EX921462
EXHAUST ACETONE
NITRIC
FILTER
IMPINGER
SAMPLE
(CU FT)
49.30
44.26
EX921451 <
EX921452 <
EX921453 <
EX921454 <
LEAD
(ug)
0
5
2.5
0.5
2.5
0.5
ZINC STRONTIUM
(ug) (ug)
51.4
49.6
24.0
4.1 <
1.3 <
22 <
0.93
0.58
0.93
0.2
0.5
0.2
CHROMIUM SAMPLE
(ug) (N3)
16.73
30.83
1.08
2.00
0.65
13.00
.395
.253
.395
.395
.395
.395
LEAD ZINC STRONTIUM CHROMIUM
(ug/H3) (ug/M3) (ug/M3) (ug/M3)
< MDL
4.0
< MDL
< HDL
< HDL
< MDL
36.8
39.6
17.2
2.9
0.9
15.8
0.7
0.5
0.7
< HDL
< HDL
< HDL
12.0
24.6
0.8
1.4
0.5
9.3
-------
TEST: METALS f5 TRAVIS AFB
DATE: 06-26-92 AM2 PAINT BOOTH TESTS
METHOD: NIOSH 7300 ACUREX PROJECT 8485
Non paint time deducted
ACUREX BASE PRE-CAL POST-CAL
GRID LOC SAMPLE * SAMPLE * PUMP * (ml/min) (ml/min)
RECIRC ACETONE
NITRIC
FILTER
IMPINGER
RUN TIME
(min)
EX921459 <
EX921460 <
EX921461 <
EX921462 <
LEAD
(ug)
2.5
0.5
2.5 <
0.5
PAINT:
OBJECT:
ZINC
(ug)
13
7.6
1.25
29
GUNSHIP GRAY POLY
THRUST REVERSER
STRONTIUM
(ug)
0.58
< 0.2
< 0.5
< 0.2
CHROMIUM
(ug)
3.2
7.60
1.03
19.00
AVG FLOW
(L/MIN)
1.253
1.253
1.253
1.253
LEAD
(ug/M3)
< MDL
< MDL
< MDL
< MDL
D E INITIALS:
0 A INITIALS:
ZINC
(ug/M3)
10.4
6.1
< MDL
23.2
STRONTIUM
(ug/M3)
0.5
< MDL
< MDL
< MDL
LJL
CHROMIUM
(ug/M3)
2.6
6.1
0.8
15.2
-------
TEST: METALS *5
DATE: 06-26-92 AM2
METHOD: NIOSH 7300
Non paint time deducted
GRID CHART 1 - LEAD
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
< MDL
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
0.4
1234
< MDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< MDL < MDL < MDL < MDL
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL < MDL < MDL < MDL
17 18 19 20
< MDL < MDL < MDL < MDL
< MDL
INLET GRID B
IB
< MDL
28
< MDL
38
< MDL
PAINT TYPE: GUNSHIP GRAY POLY UNITS: ug/M3
OBJECT: THRUST REVERSER OSHA TWA: 50 ug/M3
GRID MDL: 0.075 ug/SAMPLE
PAINTER MDL: 0.075 ug/SAMPLE
EXHAUST DUCT: < MDL
RECIRC DUCT: 4.0
-------
TEST: METALS 05
DATE: 06-26-92 AM2
METHOD: NIOSH 7300
Non paint time deducted
GRID CHART 2 - ZINC
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
0 A INITIALS: 0
Painter Over
3.2
Painter Under
2.9
INLET GRID A
1A
2.0
2A
29.0
3A
18.4
EXHAUST GRID
1234
4.6 1.7 1.5 1.7
5 A 7 ft
2.3 < MDL 22.7 1.7
2.4
9 10 11 12
2.7 3.1 34.9 42.7
21 22 23 24
1.9 2.4 3.8 1.6
13 14 15 16
1.5 2.9 1.6 2.8
17 18 19 20
3.4 2.8 10.7 3.3
3.4
INLET GRID B
18
3.9
28
3.9
38
2.1
PAINT TYPE: GUNSHIP GRAY POLY UNITS: ug/W
OBJECT: THRUST REVERSER OSHA TWA: 1000 ug/M3
GRID MDL: 0.3 ug/SANPLE
PAINTER MDL: 0.3 ug/SAMPlE
EXHAUST DUCT: 36.8
RECIRC DUCT: 39.6
-------
TEST: METALS *5
DATE: 06-26-92 AM2
METHOD: NIOSH 7300
Non paint time deducted
GRID CHART 3 - STRONTIUM
Painter Over
5.0
Painter Under
< HDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
EXHAUST GRID
0 E INITIALS: LJL
0 A INITIALS:
1 2
< MDL < MDL
5 6
< MDL < MDL
< MDL
9 10
< MDL < MDL
21 22
< MDL < MDL
13 U
< HDL < MDL
17 ' 18
< MDL < MDL
3 4
< MDL < MDL
7 8
< MDL < MDL
11 12
< MDL < MDL
23 24
< MDL < MDL
15 16
< MDL < MDL
o
19 20
< MDL < MDL
< MDL
PAINT TYPE: 6UNSHIP GRAY POLY UNITS: ug/M3
OBJECT: THRUST REVERSER OSHA TWA: 50 ug/M3
GRID MDL: 0.3 ug/SANPLE
PAINTER MDL: 0.3 ug/SAMPLE
INLET GRID B
IB
< MDL
28
< MDl
38
< MDL
EXHAUST DUCT:
RECIRC DUCT:
0.7
0.5
-------
TEST: METALS #5
DATE: 06-26-92 AH2
METHOD: NIOSH 7300
Mon paint time deducted
GRID CHART 4 - CHROMIUM
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8485
D E INITIALS: LJL
Q A INITIALS: 0
Painter Over
3.5
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
< MDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< HDL < MDL < MDL 1.1
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL < MDL 1.8 2.1
17 18 19 20
2.8 < MDL 1.7 < MDL
1.5
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
PAINT TYPE: GUNSHIP GMT POLY UNITS: ug/N3
OBJECT: THRUST REVERSE* OSHA TWA: 50 ug/M3
GRID MDL: 0.3 ug/SAMPLE
PAINTER MDL: 0.3 ug/SAMPLE
EXHAUST DUCT: 12.0
RECIRC DUCT: 24.6
-------
TEST: ISOCYANATES *1 TRAVIS AFB PAINT: UNITE TOPCOAT
DATE: 06-23-92 AM PAINT BOOTH TESTS OBJECT: COMFORT PALLET
METHOD: OSHA 42/NIOSH 5521 Printed: 24-Sep
ACUREX BASE PRE-CAL POST-CAL RUN TIME HD1
GRID LOG FILTER * SAMPLE * PUMP * (ml/min) (ml/min) (min) (ug)
1
2
3
4
5
6
7
8
9
10
11
12
12 DUP
21
22
23
24
13
14
15
15 DUP
16
17
18
19
20
P over
P under
1A
2A
3A
1B
2B
3B
F BLANK
EXHAUST 1
RECIRC 1
19
21
9
4
14
20
6
13
12
5
8
17
25
33
16
10
1
30
23
31
35
26
27
34
24
22
0051 Imp
00501*?
18
29
28
11
32
15
0049<«p
0048lRp
EX920714
EX920715
EX920716
EX920717
EX920718
EX920719
EX920720
EX920721
EX920722
EX920723
EX920724
EX920725
EX920739
EX920726
EX920727
EX920728
EX920729
EX920730
EX920731
EX920732
EX920738
EX920733
EX920734
EX920735
EX920736
EX920737
EX920051
EX920050
EX920708
EX920709
EX920710
EX920711
EX920712
EX920713
EX920049
EX920048
41
13
4
35
33
12
20
29
15
18
10
14
43
11
24
9
34
40
2
25
42
5
1
17
7
23
19
30
3
28
27
32
31
22
36
37
927
979
1009
974
999
945
975
992
993
969
987
945
995
1001
979
993
993
995
993
935
1003
990
990
990
952
1034
984
962
990
970
965
948
937
942
915
951
920
1058
1000
990
1018
977
981
975
1019
987
1056
945
970
1036
1015
1045
985
1011
1040
971
1008
1004
1005
996
1160
1056
963
1024
987
981
963
929
932
995
939
1053
60
58
60
60
60
60
60
60
60
60
61
60
60
60
60
62
60
60
46
60
60
61
60
60
60
60
59
59
59
59
59
59
59
52
51
52
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
16
0.2
ND
ND
ND
ND
ND
ND
0.8
0.9
D E by:
0 A by:
AVG FLOW
(L/MIN)
0
1
1
0
1
0
0
0
1
0
1
0
0
1
0
1
0
1
1
0
1
0
0
0
1
1
0
0
Q
0
0
0
0
0
0
0
1
.924
.019
.005
.982
.009
.961
.978
.984
.006
.978
.022
.945
.983
.019
.997
.019
.989
.003
.017
.953
.006
.997
.998
.993
.056
.045
.974
.993
.989
.976
.964
.939
.935
.969
.000 n
.927
.002
BN
HDI
(ug/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
< HDL
< HDL
< HDL
< MDL
< HDL
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
278.6
3.4
< HDL
< HDL
< HDL
< HDL
< HDL
< MDL
o sanple
16.9
17.3
-------
TEST: ISOCYANATES *1
DATE: 06-23-92 AM
METHOD: OSHA 42/NIOSH 5521
GRID CHART 4 - HOI
TRAVIS AFB
PAINT BOOTH TESTS
EXHAUST GRID
D E INITIALS: BN
0 A INITIALS: 0
Painter Over
278.6
Painter Under
3.4
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
1234
< MDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
9 10 11 12
< MDL < MDL < MDL < MDL
< MDL
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL < MDL < MDL < MDL
< MDL
17 18 19 20
< MDL < MDL < MDL < MDL
INLET GRID B
IB
< MDL
28
< MDL
38
< MDL
PAINT TYPE: WHITE TOPCOAT
OBJECT: COMFORT PALLET
UNITS: ug/KJ GRID MDL: 0.5 ug/SAMPLE
OSHA TWA: 40 ug/M3 PAINTER MDL: 0.05 ug/SAMPLE
EXHAUST DUCT: 16.9
RECIRC DUCT: 17.3
-------
TEST: ISOCYANATES «2 PAINT: WHITE TOPCOAT
DATE: 06-25-92 AH2 OBJECT: BRAKE PARTS & RAMP
HETHOD: OSHA 42/NIOSH 5521
TRAVIS AFB PAINT BOOTH TESTS
ACUREX BASE PRE-CAL POST-CAL RUN TIME
GRID LOC FILTER * SAMPLE * PUMP * (ml/min) (ml/mi n) (min)
1
2
3
4
5
6
7
7DUP
8
9
10
11
12
21
22
23
24
24 DUP
13
13 DUP
14
15
16
17
18
19
20
P over
P under
1A
2A
3A
IB
28
3B
F BLANK
EXHAUST C
RECIRC C
EXHAUST I
RECIRC 1
65
60
54
36
70
63
69
53
51
2
56
64
38
58
39
42
68
3
61
49
57
50
48
44
55
7
47
0060<*>
00621MP
66
46
62
52
43
40
45
67
37
0063i«p
0061 lip
EX9206B3
EX920684
EX920685
EX920686
EX920687
EX920688
EX920689
EX920690
EX920691
EX920692
EX920693
EX920694
EX920695
EX920696
EX920697
EX920698
EX920699
EX920700
EX920701
EX920702
EX920703
EX920704
EX920705
EX920706
EX920707
EX920740
EX920673
EX920060
EX920062
EX920677
EX920678
EX920679
EX920680
EX920681
EX920682
EX920676
EX920671
EX920672
EX920063
EX920061
41
15
23
28
20
31
16
4
1
12
14
17
40
25
43
29
10
18
11
22
13
21
24
7
42
5
34
33
35
3
6
27
30
19
8
26
2
32
36
39
948
993
1040
991
968
1002
979
1096
1000
941
1023
998
990
995
1007
1013
988
1017
982
971
964
1000
970
988
1019
1007
1048
1045
1005
993
1000
1057
981
1008
980
1000.2
1007
1013
1058
1003
964
1005
1048
1006
972
1000
1000
1093
981
973
1078
1005
995
1019
993
1020
973
1026
1008
1036
1014
1003
1017
1014
1016
1010
1052
1060
1016
975
1008
1071
999
1015
959
1012.114
1039
996
1038
1069
66
67
66
65
66
66
66
66
66
66
66
66
65
66
66
65
66
66
67
57
64
65
66
66
65
66
65
65
65
66
66
66
65
66
66
65.48571
58
59
58
59
HDI
(ug>
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
0.8
ND
ND
ND
ND
ND
ND
3
0.2
ND
HD
ND
ND
ND
ND
0.5
ND
ND
2
0.2
DE by: LJL
QA by:
Printed: 24-Sep
AVG FLOW HDI
(L/MIN) (ug/H3)
0.956
0.999
1.044
0.9985
0.97
1.001
0.9895
1.0945
0.9905
0.957
1.0505
1.0015
0.9925
1.007
1
1.0165
0.9805
1.0215
0.995
1.0035
0.989
1.0015
0.9935
1.001
1.0175
1.0085
1.05
1.0525
1.0105
0.984
1.004
1.064
0.99
1.0115
0.9695
1.006157
1.023
1.0045
1.048
1.036
< MDL
< MDL
< MDL
< HDL
< MDL
< MDL
< HDL
< HDL
< MDL
< MDL
< MDL ,
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
12.6
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
43.9
3.0
< MDL
< MDL
< MDL
< HDL
< HDL
< HDL
7.6
< MDL
< HDL
32.9
3.3
-------
01
TEST: ISOCYANATES #2
DATE: 06-25-92 AM2
METHOD: OSHA 42 & NIOSH 5521
GRID CHART 3 - HOI
TRAVIS AFB
PAINT BOOTH TESTS
EXHAUST GRID
D E INITIALS: 0
0 A INITIALS: 0
printed: 24-Sep
Painter Over
43.9
Painter Under
3.0
INLET GRID A
1A
< MDL
2A
< M>L
3A
< MDL
1234
< MDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< HDL < MDL < MDL < MDL
21 22 23 24
< MDL < MDL < MDL < MDL
< MDL
13 14 15 16
< MDL 12.6 < MDL < MDL
< MDL
U 18 19 20
< MDL < MDL < MDL < MDL
Field Blank
7.6
Nominal
value
INLET GRID B
IB
< MDL
28
< MDL
38
< MDL
PAINT TYPE: WHITE TOPCOAT
OBJECT: BRAKE PARTS I RAMP
UNITS: UB/M3
OSHA TUA: 40 ug/M3
GRID MDL: 0.5 ug/SAMPLE
PAINTER MDL: 0.05 ug/SAMPLE
EXHAUST DUCT: < MDL CASSETTE
32.9 IMPINGER
RECIRC DUCT: < MDL CASSETTE
3.3 IMPINGER
-------
TEST: ISOCYAMATES #3 TRAVIS AFB
DATE: 06-25-92 PM PAINT BOOTH TESTS
METHOD: OS HA 42 t NIOSH 5521 ACUREX PROJECT 8463
ACUREX BASE PRE-CAL POST-CAL RUN TIME
GRID LOG FILTER* SAMPLE * PUMP * (ml/min) (ml/min) (min)
1
2
3
I
5
6
6 DUP
7
8
9
10
11
11 DUP
12
21
22
23
24
13
14
14 DUP
15
16
17
18
19
20
P over
P under
U
2A
3A
1B
2B
3B
F BLANK
EXHAUST C
RECIRC C
EXHAUST 1
RECIRC 1
73 EX920537
94 EX920538
77 EX920539
78 EX920540
84 EX920541
88 EX920542
89 EX920567
82 EX920543
79 EX920544
92 EX920545
85 EX920546
91 EX920547
86 EX920568
95 EX920548
76 EX920557
97 EX920558
71 EX920559
98 EX920560
96 EX920549
101 EX920550
100 EX920569
87 EX920551
99 EX920552
103 EX920553
93 EX9205S4
80 EX920555
90 EX920556
0054inp EX920054
0055 iw> EX920055
83 EX920561
102 EX920S62
75 EX920563
74 EX920564
72 EX920565
105 EX920566
13
12
28
24
31
21
11
1
20
14
29
4
22
41
23
16
10
25
15
17
7
18
34
43
42
5
40
35
33
6
27
3
30
19
8
1014
973
1006
1017
1000
1003
1008
981
972
1078
1020
1093
1036
964
1048
1000
973
1019
1005
1005
1014
1026
1052
993
1016
1010
995
1016
1060
1008
1071
975
999
1015
959
1018
978
1011
1029
1001
997
1008
980
968
1074
1016
1104
1067
951
1046
1002
1045
1024
1004
1000
1017
1024
1050
995
1013
1003
989
1022
1063
1009
1073
986
996
1008
978
56
58
57
58
57
58
58
58
58
58
58
58
50
59
58
58
58
58
58
58
58
58
58
58
57
59
57
57
57
58
58
58
58
58
58
PAINT:
OBJECT:
TO I
(ug)
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
CAMEL GRAY
AIR SPLITTERS
MDI HDI
(ug) (ug)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
0.6
NO
ND
1
0.2
ND
ND
ND
ND
ND
ND
D E INITIALS:
0 A INITIALS:
AVG FLOW TDI MDI
(L/MIN) (ug/M3) (ug/M3)
1.016 < MDL
0.9755 < MDL
1.0085 < MDL
1.023 < MDL
1.0005 < MDL
1 < MDL
1.008 < MDL
0.9805 < MDL
0.97 < MDL
1.076 < MDL
1.018 < MDL
1.0985 < MDL
1.0515 < MDL
0.9575 < MDL
1.047 < MDL
1.001 < MDL
1.009 < MDL
1.0215 < MDL
1.0045 < MDL
1.0025 < MDL
1.0155 < MDL
1.025 < MDL
1.051 < MDL
0.994 < MDL
1.0145 < MDL
1.0065 < MDL
0.992 < MDL
1.019 < MDL
1.0615 < MDL
1.0085 < MDL
1.072 < MDL
0.9805 < MDL
0.9975 < MDL
1.0115 < MDL
0.9685 < MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
LJL
HDI
(ug/M3)
< NDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
10.4
< MDL
< MDL
17.2
3.3
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
0 no sanpleno MMpleno sample
104 EX920535
81 EX920536
37inp EX920037
39i«p EX920039
2
32
36
39
1039
996
1038
1069
1061
989
1058
1086
51
52
51
52
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
0.5
0.2
1.05 < MDL
0.9925 < MDL
1.048 < MDL
1.0775 < MDL
< MDL
< MDL
< MDL
< MDL
< NDL
< MDL
9.4
3.6
-------
TEST: ISOCYANATES *3
DATE: 06-25-92 PM
METHOD: OSHA 42 & NIOSH 5521
GRID CHART 3 - HOI
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8463
D E INITIALS: 0
0 A INITIALS: 0
Painter Over
17.2
Painter Under
3.3
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
EXHAUST GRID
1234
< MDL < MDL < MDL < MDL
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< MDL < MDL < MDL < MDL
< MDL
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< HDL < MDL < MDL < MDL
< MDL
17 18 19 20
< MDL 10.4 < MDL < MDL
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
-------
TEST: ISOCYANATES #4
DATE: 06-30-92 AN1
METHOD: OSHA 42 & NIOSH 5521
ACUREX BASE
GRID LOG SAMPLE * SAMPLE * PUMP *
1 148 EX920578
2 156 EX920579
3 159 EX920580
4 151 EX920581
5 174 EX920582
6 152 EX920583
6 DUP 155 EX920584
7 157 EX920585
8 147 EX920586
9 154 EX920587
10 173 EX920588
11 168 EX920589
12 165 EX920590
21 169 EX920591
22 160 EX920592
23 150 EX920593
24 145 EX920594
13 164 EX920595
14 172 EX920S96
15 162 EX920597
16 153 EX920598
17 171 EX920599
18 161 EX920600
19 163 EX920601
20 175 EX920602
20 DUP 167 EX920603
P over 581 *p EX920058
P under 59inp EX920059
1A 143 EX920571
2A 149 EX920572
3A 166 EX920573
IB 158 EX920574
IB DUP 141 EX920575
2B 170 EX920576
3B 142 EX920577
F BLANK 0040in> EX920040
F BLANK 146 EX920570
EXHAUST C 144 EX920532
RECIRC C 214 EX920531
EXHAUST 1 57iip EX920057
RECIRC I 56««p EX920056
14
45
34
31
1
19
51
17
49
11
55
43
13
25
21
18
54
24
42
28
16
5
32
50
29
30
48
46
47
12
33
40
6
35
20
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8463
PRE-CAL POST-CAL RUN TIME
(ml/min) (ml/min) (min)
970
1042
1010
1054
990
1023
1031
1023
993
1017
1021
1021
987
1023
1029
1011
1030
985
1020
1045
1046
1021
1015
1015
1037
1045
997
987
1011
949
1016
1028
1033
1033
955
950
1014
994
1066
944
1001
994
1263
980
1032
988
977
1002
1056
1005
996
998
1033
1004
1019
1060
1004
982
982
1006
1025
985
974
1001
964
1004
1015
1039
1036
941
noilnal values
9
52
53
36
39
noMinal values
1002
998
961
962
994
960
952
940
61
61
61
61
62
61
61
61
61
62
61
61
60
61
61
61
61
61
61
61
61
62
61
61
61
61
61
61
61
61
61
61
61
61
61
60
60
55
55
55
55
PAINT:
OBJECT:
TDI
(ug)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
NO
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
NO
DARK GRAY TOPCOAT
QEC PANELS (PLANE SIDING)
MDI HDI AVG FLOW
(ug) (ug) (L/HIN)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
0.5
0.8
ND
ND
NO
0.5
NO
ND
1
ND
ND
ND
ND
ND
ND
ND
NO
0.2
ND
NO
ND
1
0.2
0.96
1.028
1.002
1.06
0.967
1.012
1.0125
1.143
0.9865
4.0245
1.0045
0.999
0.9945
1.0395
1.017
1.0035
1.014
1.009
1.012
1.032
1.053
1.0125
0.9985
0.9985
1.0215
1.035
0.991
0.9805
1.006
0.9565
1.01
1.0215
1.036
1.0345
0.948
1
1
0.998
0.979
0.9565
0.951
D E INITIALS:
0 A INITIALS:
TDI MDI
(ug/M3) (ug/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
LJL
HDI
(ug/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
8.1
12.7
< MDL
< MDL
< MDL
8.2
< MDL
< MDL
16.5
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
3.3
< MDL
< MDL
< MDL
19.0
3.8
-------
5T: ISOCYANATES *
rE: 06-30-92 AMI
DO: OSHA 42 I NIO!
CHART 4 - HOI
Painter Over
16.5
Painter Under
< MDL
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
>H 5521
TRAVIS AFB 1
PAINT BOOTH TESTS I
ACUREX PROJECT 8463
EXHAUST GRID
1234
< HDL < MDL < MDL < MDL
5678
< MDL < MDL < MDL < MDL
< MDL
9 10 11 12
< MDL < MDL < MDL < MDL
21 22 23 24
< MDL < MDL < MDL < MDL
13 14 15 16
< MDL 8.1 12.7 < MDL
17 18 19 20
< MDL < MDL 8.2 < MDL
< MDL
) E INlTIi
1 A 1MITI/
(LS: LJL
M.S:
Field Blank
IMP 3.3
FILT <: MDL
nominal values
INLET GRID B
1B
< NDL
< MDL
2B
< MDL
38
< NDL
PAINT TYPE: DARK GRAY TOPCOAT UNITS: ug/M3 GRID MDL: 0.5 ug/SAMPLE
OBJECT: OEC PANELS (PLANE SIDING) OSHA TWA: 40 ug/M3 PAINTER MDL: 0.05 ug/SAMPLE
EXHAUST DUCT: < HDL CASSETTE
19.0 IMPIHGER
RECIRC DUCT: < MDL CASSETTE
3.8 INPINGER
Note: The field (solution) blank for NIOSH 5521 (used on the painter and duct samples) contained 0.2 ug. or a nominal 3.3
ug/M3 for a 60 Minute test at 1 liter/Bin. The sample levels here are calculated in terms of actual volume and tine.
-------
TEST: ISOCYAMATES *5 TRAVIS AFB
DATE: 06-30-92 AM2 PAINT BOOTH TESTS
METHOD: OSHA 42 & NIOSH 5521 ACUREX PROJECT 8463
ACUREX BASE PRE-CAL POST-CAL RUN TINE
GRID LOG SAMPLE * SAMPLE ff PUMP * (ml/fflin) (ml/min) (min)
1
2
3
3 DUP
4
5
6
7
8
9
10
11
12
21
22
22 DUP
23
24
13
14
15
16
17
17 DUP
18
19
20
P over
P under
1A
2A
3A
IB
2B
3B
F BLANK
EXHAUST 1
EXH 1 dup
RECIRC C
RECIRC I
116 EX920610
139 EX920611
140 EX920612
107 EX920613
124 EX920614
131 EX920615
121 EX920616
126 EX920617
115 EX920618
122 EX920619
114 EX920620
130 EX920621
129 EX920622
120 EX920623
109 EX920624
134 EX920625
135 EX920626
123 EX920627
108 EX920628
125 EX920629
110 EX920630
127 EX920631
136 EX920632
138 EX920633
111 EX920634
133 EX920635
118 EX920636
41inp EX920041
42f«p EX920042
128 EX920604
137 EX920605
119 EX920606
106 EX920607
117 EX920608
112 EX920609
113 EX920534
43 lap EX920043
44i*p EX920044
132 EX920533
45 l*p EX920045
30
40
14
25
1
6
47
17
32
13
20
28
21
16
34
5
33
42
29
12
18
45
35
11
43
50
24
48
46
31
49
54
19
51
55
9
36
52
S3
39
1025
1015
950
1056
944
1039
1001
954
982
1002
941
1019
1005
1060
994
1004
1004
1004
1006
964
996
1014
1036
1032
977
982
1033
985
974
1066
980
998
1001
994
988
0
952
985
960
940
1013
1010
952
1066
952
1071
1000
947
1007
1010
955
1037
1013
1076
996
1001
1008
1009
1011
986
1000
1033
1031
1029
992
975
1050
994
996
1063
984
997
1000
1030
984
0
956
1082
996
1010
56
56
57
57
57
56
56
56
56
55
56
56
56
56
56
57
56
56
56
56
56
57
56
57
56
56
57
56
56
56
56
56
56
56
56
60
51
51
52
52
PAINT:
OBJECT:
TDI
(ug)
NO
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
NO
ND
PRIMER
PLANE ENGINE
MDI HD1
(ug) (ug)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
HO
ND
ND
NO
NO
NO
ND
NO
ND
ND
NO
ND
ND
NO
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
NO
ND
ND
ND
ND
ND
ND
NO
ND
NO
NO
ND
ND
ND
ND
ND
ND
NO
ND
ND
NO
ND
0.2
0.2
NO
ND
0 »
HO
ND
NO
ND
0.2
0.2
NO
0.2
AVG FLOW
(L/MIN)
1.019
1.0125
0.951
1.061
0.948
1.055
1.0005
0.9505
0.9945
1.006
0.948
1.028
1.009
1.068
0.995
1.0025
1.006
1.0065
1.0085
0.975
0.998
1.0235
1.0335
1.0305
0.9845
0.9785
1.0415
0.9895
0.985
1.0645
0.982
0.9975
1.0005
1.012
0.986
1
0.954
1.0335
0.978
0.975
D E INITIALS:
0 A INITIALS:
TDI MDI
(ug/M3) (ug/M3)
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< HDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
LJL
HOI
(ug/M3)
< MDL
< MDL
< MDL
< MDL
MDL
MDL
MDL
MDL
MDL
MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
3.6
3.6
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
< MDL
4.1
3.8
< MDL
3.9
-------
Ol
TEST: ISOCTANATES *5
DATE: 06-30-92 AM2
METHOD: OSHA 42 I NIOSH 5521
GRID CHART 3 - HDI
TRAVIS AFB
PAINT BOOTH TESTS
ACUREX PROJECT 8463
EXHAUST GRID
D E INITIALS: LJL
Q A INITIALS:
Painter Over
3.6
Painter Under
3.6
INLET GRID A
1A
< MDL
2A
< MDL
3A
< MDL
1234
< HDL < MDL < MDL < MDL
< MDL
5678
< MDL < MDL < HDL < MDL
9 10 11 12
< MDL < MDL < HDL < MDL
21 22 23 24
< MDL < MDL < MDL < MDL
< MDL
13 14 15 16
< MDL < MDL < MDL < MDL
17 18 19 20
< MDL < MDL < MDL < MDL
< MDL
Field Blank
< MDL
INLET GRID B
IB
< MDL
2B
< MDL
3B
< MDL
PAINT TYPE: PRIMER
OBJECT: PLANE ENGINE
UNITS: ug/M3
OSHA TWA: 40 ug/W
GRID MDL: 0.5 ug/SANPLE
PAINTER MDL: 0.05 ug/SAMPLE
EXHAUST DUCT: 4.1 IMPINGER
EXHAUST DUCT OOP: 3.8 IMPINGER
RECIRC DUCT: < MDL CASSETTE
3.9 IMPINGER
Note: Prtaer does not contain isocyanates, however, the field (solution) blank for NIOSH 5521 (used on the painter and duct samples)
contained 0.2 ug, or a nominal 3.3 ug/M3 for a 60 ninute test at 1 liter/win. The level seen on the painter and duct samples
here is the same 0.2 ug/sanple calcualted in terns of the volune saopled.
-------
APPENDIX H
QUALITY ASSURANCE/QUALITY CONTROL EVALUATION
A number of quality assurance/quality control (QA/QC) procedures were followed to
assess the quality of the reported data. The data quality objectives (DQOs) are listed in
Table H-1. The DQOs, defined in terms of measurement accuracy, precision, and completeness.
were originally outlined in the Quality Assurance Project Plan (Reference 1 ). In response to the
EPA QA review (Reference 2 ), the DQOs were subsequently revised and submitted in the
Acurex Environmental letter dated 6 May 1992 (Reference 3). The high variability of normal
booth operations causes difficulty in establishing DQOs.
A. ASSESSMENT OF OVERALL DATA QUALITY
The DQO results are presented in Table H-2. Nearly all DQOs were achieved. Some
objectives, for the integrated sampling, were not met for side-by-side duplicate samples taken
at specific sampling locations. The variability detected from side-by-side duplicate analyses was
due to sample orientation. Great effort was expended to ensure that the duplicate VOC,
parliculate, isocyanates, and metals sample systems had identical orientations. However, some
samplers shifted slightly during painting.
1. Precision
To ensure data precision, air flow rate anemometer measurements at the booth
exhaust and intake faces were obtained following each test. Duplicate anemometer
measurements were taken at one randomly selected grid site per test. Split-flow duct flow rale
measurements were taken according to EPA Method 2 prior to each sampling event. A duplicate
measurement was taken every 2 days. Due to cyclonic flow patterns in the recirculation duct,
it was not possible to measure the flow rate of the recirculaled airstream using EPA Method 2.
Therefore, the precision is undefinable.
To assess the precision of GEM sampling, the periodic zero, span, and reference gas
response results were compared.
To assess precision of the integrated pollutant concentration measurements in the
booth, duplicate samples were collected during each sampling event. Because sample collection
occurred under dynamic operating conditions, a side-by-side sampling strategy was adopted to
generate the required duplicates. The side-by-side samples were located and oriented as close
to identically as possible, but under normal booth operating conditions the sampling system
often shifted during the test. For this reason, the RPD at specific sampling locations was
observed to be as high as 100 percent. However, when averaged over all the duplicate samples,
the precision RPD DQO was met for each pollutant category.
Side-by-side duplicate samples were also collected in the Integrated duct organic and
isocyanale sampling events. Precision for EPA Method 5 and the Draft Multiple Melals trains
could not be assessed because setting up side-by-side duplicate sampling trains was not
possible.
158
-------
TABLE H-1. DATA QUAUTY OBJECTIVES.
Measurement
Parameter
Volume Flow
Exhaust and intake faces
Ventilation ducts
Participate
Exhaust and intake faces and painter
Ventilation ducts
Metals
Exhaust and intake faces and painter
Ventilation ducts
Organics
Integrated
Continuous
Isocyanates
Exhaust and intake faces and painter
Ventilation ducts
Paints
% Volatile
Usage rate
Density
Measurement
Method
ACGIH
Anemometer
EPA Method 2
NIOSH 500
EPA Method 5
NIOSH 7300
Draft EPA
Multiple Metals
NIOSH 1300
EPA Method 25A
BAAQMD ST-7
OSHA 42
NIOSH 5521
Grab sample,
wt. loss on drying
Observation,
gravimetric analysis
Grab sample,
wt/vol analysis
Precision
(RPD)
20
20
35
NMC
35
NMd
35
20
20
35
35
20
NMe
20
Accuracy
(% Recovery)
±40
±10
NM"'b
NMC
±30
±30
±30
±20
±20
±30
±30
±20
NMe
±20
Completeness
(%)
90
90
90
90
90
90
90
90
90
90
90
90
90
90
aNM = Not measured; not measurable.
bMethod states that the bias is not significant.
cThe primary error source is non-isokineticrty. The isokineticty objective is 90 to 110 percent.
d Precision (as relative standard deviation) listed in the method ranges between 10 and 25 percent.
"Not definable. Estimated at ±50 percent.
159
-------
TABLE H-2 DATA QUALITY RESULTS.
Measurement Parameter
Volume Flow
Exhaust and intake faces
Exhaust duct
Recirculation duct
Particulate
Exhaust and intake faces and painter
Ventilation ducts
Metals
Exhaust and intake faces and painter
Ventilation ducts
Organics
Integrated
Continuous
Isocyanates
Exhaust and intake faces and painter
Ventilation ducts
Paints
% Volatile
Usage rate
Density
Measurement
Method
ACGIH
Anemometer
EPA Method 2
EPA Method 2
NIOSH500
EPA Method 5
NIOSH 7300
Draft EPA
Multiple Metals
NIOSH 1300
EPA Method 25A
BAAQMD ST-7
OSHA 42
NIOSH 5521
Grab sample,
wt. loss on drying
Observation,
gravimetric
analysis
Grab sample,
wt/vol analysis
Precision
(RPD)
5
5
NMb
32
NMd
23
NMe
24
10
10
10
10
5
NM9
2
Accuracy
(% Recovery)
NMa'b
±2
NMb
NMC
NMd
±15
±20
±30
±10
±10
NMf
±18
±13
NM0
±9
Completeness
(%)
95
95
NMb
90
90
90
90
86
90
90
95
90
100
90
100
aNM = Not measured; not measurable.
bFlow rate is not measurable due to cyclonic flow patterns in the duct
cMethod states that the bias is not significant.
dThe primary error source is non-isokineticrty. The isokineticrty objective is 90 to 110 percent.
"Precision (as relative standard deviation) listed in the method ranges between 10 and 25 percent.
'Spike analysis not conducted.
9Not definable. Estimated at ±50 percent
160
-------
To assess precision of the paint percent volatile and density measurements, duplicate
samples were collected and analyzed. The paint usage rate was determined gravimetrically.
There is no practical method for assessing the precision or accuracy of this measurement.
2. Accuracy
Due to cyclonic flow patterns in the recirculation duct, the relative accuracy of the air
flow rate measurements in the booth was not quantifiable. The accuracy of the measurement
of the split-flow duct flow rate according to EPA Method 2 was established using calibrated
standard pitot tubes.
To measure accuracy of the continuous organic concentration measurement, a mid-
range standard reference gas that was not a zero or span gas was used. A solvent mass
balance calculation provided an additional means of measuring accuracy, by comparing the
quantity of solvent released into the booth to the quantity measured by the continuous monitors
in the exhaust streams.
Accuracy of the metals sampling at the exhaust and intake faces was measured
through the spike and recovery of filter samples according to NIOSH 7300. NIOSH 1300
sampling accuracy was measured through the spike and recovery analysis of unused sample
tubes. The spike compounds and concentrations were selected based on the paint solvents
measured in the charcoal tubes. Spike and recovery analyses of particulate samples were not
possible. For the exhaust and intake faces and the painter, accuracy for particulate sampling
was not measurable. For the ventilation ducts, particulate measurement was also not
measurable because the primary error source is non-isokineticity. The isokineticity objective is
90 to 110 percent.
OSHA Method 42 was followed in the analysis of isocyanate compounds obtained
at the exhaust face and in the vicinity of the painter. The method does not call for spike and
recovery samples, and such were therefore not performed. Instead, isocyanates standards were
tracked to watch for instrument drift, loss of column performance, and other errors. In addition,
four standards for each analyte were run at both the beginning and end of each analytical run.
For NIOSH 5521, the laboratory obtained percent recovery data by spiking samples with urea.
To assess the accuracy of the paint percent volatile and density measurements,
published values from MSDSs for these parameters were obtained from manufacturers and
compared to the analytical results. Usage rate accuracy was not measurable.
3. Completeness
The 90-percent completeness DQO was selected based on the successful completion
of similar projects in the past involving paint spray booth emissions sampling and evaluation.
A completeness level of 90 percent ensured that sufficient valid data of known quality were
collected to evaluate project success. A completeness of 90 percent was achieved in all of the
sampling events, with the exception of the integrated organic sampling, in which an 85-percent
completeness was achieved, rather than the projected 90-percent, due to the malfunction of the
pumps used in the NIOSH 1300 sampling procedures.
161
-------
B. QUAUTATIVE DATA QUALITY OBJECTIVES
The painting operations in the booth were highly variable and non-repetitious. Therefore,
a primary concern was that the samples collected be representative of typical operations. For
this reason, sampling occurred over a 3-week period.
Careful scheduling with the paint spray booth operator was required for the successful
completion of this project. Acurex Environmental coordinated with the Travis AFB personnel to
ensure that there was a sufficiently large workpiece backlog for each test series. Acurex
Environmental also endeavored to ensure that a representative sample of each typical workpiece
was evaluated.
C. REFERENCES
1. Hughes, S. E. and Ayer, J., Category III Quality Assurance Project Plan (QAPR. Acurex
Environmental Corporation, Mountain View, California, prepared for U.S. Environmental
Protection Agency, EPA Contract No. 68-D1 -0146, Work Assignment 0/004, AEERL, Research
Triangle Park, NC, March 1992.
2. EPA Quality Assurance Review of the Category III QAPP, EPA Contract No. 68-D1-0146, Work
Assignment 0/004, April 1992.
3. Hughes, S. E. and Wolbach, C. D., Response to EPA Quality Assurance Review,
May 6, 1992.
162
-------
APPENDIX I
ECONOMIC CALCULATIONS
163
-------
Economic Evaluation
Page 1 of 4
Percent Recirc
SUMMARY TABLE
Costs for Incineration Devices with 35% heat recovery (Thousands of dollars)
Flowrate Thermal Incineration Catalytic Incineration
dscfm Capital Cost Annual O&M Cost Capital Cost Annual O&M Cost
0 30000
50 15000
75 7500
90 3000
$392
$387
$333
$275
$383
$232
$147
$91
$550
$471
$368
$270
$297
$192
$127
$81
-------
Economic Evaluation Page 2 of 4
ASSUMPTIONS
Capital cost for recirc/split-flow modification: $60,000
VOC concentration in the exhaust increases linearly as the % recirc increases
Net heat of combustion of volatile compounds is approximately 3000 Btu/scf
Exhaust Stream Characteristics
[VOC] heat content
(ppm) (Btu/scf) (Btu/lb)
% recirc 10 0.03 0.41
0 20 0.06 0.81
50 40 0.12 1.62
75 100 0.3 4.06
90
All calculations based on "Control Technologies for Hazardous Air Pollutants", EPA/625/6-91/014, June 1991.
Calcs. in the manual are based on April 1988 dollars. Convert to August 1992 $ with the following CE Equipment Indices:
Apr. 1988 CE Equipment Index: 369.4
Aug. 1992 CE Equipment Index: 390.8
Assume 10 year equipment lifetime and 10% annual interest rate.
Operating hours 40 hrs/wk
50 wks/yr
Methane fuel cost $3.30 per 1000 cf
Electricity cost $0.06 per kWh
O&M labor cost $14.00 per hour
Flowrate 15000dscfm
Heat Content 0.81 Btu/lb
Exhaust Temp. 77 F
-------
Economic Evaluation
Page 3 of 4
SAMPLE THERMAL INCINERATION CALCULATION
Destruction Eff.
Heat Recovery
Air Heat Cap (Cp)
Temp, into Incin
Combust, temp
98%
35%
0.253 Btu/lb-F
610F
1600 F
(the spreadsheet calcs are set for 0, 35, 50, OR 70% heat recovery]
Supplemental fuel (methane) requirements
Total flow
369.7
15369.7
Thermal Incinerator capital cost (Apr. 1988 $)
Purchased EquiprrAPITAL COSTS
Total Thermal Incin. Capital Cost (Apr. 1988$)
Convert to Aug. 1992 dollars:
Include the cost to modify duct
| TOTAL CAPITAL COST
$162,627
$191,900
$308,960
$326,858
$60,000
$386,858 I
scfm
scfm
ANNUAL OPERATING COSTS
DIRECT
Methane Fuel Cost
Pressure Drop
Electricity usage
Electricity costs
Oper. Labor Costs
Supervisory costs
Maintenance labor and mat'l costs
INDIRECT
Overhead
Administrative
Property taxes
Insurance
Capital Recovery
$146,414
8 in. H2O
44511 kWh/yr
$2,626
$1,750
$263
$3,500
$3,308
$7,737
$3,869
$3,869
$62,981
[TOTAL ANNUAL OPER. COSTS $232,447 |
-------
Economic Evaluation
Page 4 of 4
SAMPLE CATALYTIC INCINERATION CALCULATION
Temp at catalyst inlet 997 F
Temp at catalyst outlet 1000
Temp after heat recovery 400
Supplemental fuel (methane) requirements
Total flow
221.9
15221.9
scfm
scfm
Catalytic Incinerator capital cost (Apr. 1988 $)
Purchased EquiprrAPITAL COSTS
Total Incin. Capital Cost (Apr. 1988$)
Convert to Aug. 1992 dollars:
Include the cost to modify duct
L
TOTAL CAPITAL COST
$204,694
$241,538
$388,877
$411,405
$60.000
$471.405
Space Velocity
Catalyst Bed Size
Assume a 2-year catalyst life
Precious metal cost
40,000 (1/hr)
22.83 cu ft
$3,000 per cu ft
ANNUAL OPERATING COSTS
DIRECT
Methane Fuel Cost
Pressure Drop
Electricity usage
Electricity costs
Catalyst replacement cost
Oper. Labor Costs
Supervisory costs
Maintenance labor and mat'l costs
INDIRECT
Overhead
Administrative
Property taxes
Insurance
Capital Recovery
$87,863
1 0 in. H2O
55103 kWh/yr
$3,251
$39,469
$1,750
$263
$3,500
$3,308
$9,428
$4,714
$4,714
$34,118
ITOTAL ANNUAL OPER. COSTS $192,377 |
-------
APPENDIX J
EXAMPLE CALCULATION WORKSHEET FOR PERCENT RECIRCULATION
VERSUS PERCENT PARTICULATE REMOVAL EFFICIENCY
168
-------
PROJECTED POLLUTANT LEVELS WITH RECIRCULATION
This calculation assumes no split-flow.
% REMOVAL OF STRONTIUM CHROMATE
% REMOVAL OF ISOCYANATES:
85
85
RECIRCULATION RATE =
87.4%
This worksheet compares results to the TWA Em, not to the STEL
COMPOUNDS
DETECTED Current PROJECTED Booth
LEVEL W/O 8-hour TWA LEVEL Em Calculation
ORGANICS VS. Em
VOC1:
MEK
VOC2:
MIBK
VOC3:
TOLUENE
VOC4:
N-BUTYL ACETATE
VOC5:
XYLENES
VOC6:
ETHYLACETATE
VOC7:
2-BUTANOL
METAL Em CALCULATIONS
STRONT CHROMATE as Cr
ISOCYANATE Em CALCULATIONS
HDI
DIRC. PELorTLV mg/m3
/m3 mg/m3
5.80 590 '46
4.20 205 33
0.64 1
88 5
1.10 710 9
0.11 434 1
0.26 1400 2
0.28 305 2
0.0063 0
I ORGANIC Em
05 0.050
3
D00570 0.034 0.005
(dimensionless)
0.08
0.16
0.03
0.01
0.00
0.00
0.01
0.29|
Metal Em
1
HDI Em
0.13
169
(The reverse of this page is blank)
------- |