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AR226-2084
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cc: Doug Anton
KenLau
Chris Gueris
Sara Joslin
.
Jay Kennedy
Mark Lodi
Gene Mathis
Art Nelson
Dave Rurak
Janet W aters
January 1 5 ,1 9 9 8
CW CRP 711-251 Geneva A4066 Parlin C irc le v ille W W , B-21 W W , B-168 Laurel Run 2E31
W W , B-168 CRP 711
To: C-8 PA Q ETeaimm
Rik Brandenburg Bob Brown Bob Buck Bill Buxton Bob Cavanaugh Rich Chatten Dave Ettis Vinci Felix Tony Fernandes Andy Feiring Cheryl Fisher M aniG anti Dave Goehringer David G reene Ron Hemingway Hsu-Nan Huang Pete Huesmann
Ming Hung Dave Johnson M ortKatz Gerry Kennedy M att Kenings Steve Korzeniowski
Milan Kosanovich
DW C R P711/2220E
CW CRP 713 CRP 713 CRP 702 BMP 27-2234
CRP 711 CRP 702 ESL 328/231B
W W .8 1 6 8 ESL 269/200 CRP 702 CRP 702 Haskell 626A CW CRP 702 ESL 293/204 W W .B 168 C irc le v ille Haskell 314B CRP 702 CW W W , B21T
Leo Lech
W W .B 21
Earl M acFariane
BMP 17-1124'
Michio Maemori
Tokyo
Nevio Marini
CW
Marianne Marsi
CRP 702
Paul Mathur
W W .B 168
Bob Mattson
W W , B168
Niall McKee
CRP 713
John Migiiore
W W .B 1
Jim Moore
Richmond
Charles Mulder
DW
Bruno Muzzi
CW
M arcel van den Noort D W
Rob Pinchot
CRP 711-2210
Tony Playtis
W W , B24
W eiming Qiu
ESL 328/308A
Jose Rodriguez-Parada ESL 328/262
Theo Schroots
Meyrin L-2243
Jan Stouffer
W W .B 168
Hiroshi Totsuka
SW
Ted Treat
W W .B 22
R ajeevVaidya
CRP 702
Paul Wijnands
DW
Rogor*Zipf-el * W W .B 21
From? Greg Chapman - Core Team Leader, C-8 Project
Meeting Notes and Charts for the
January 6 and 7.1998 PACE Team Meetings
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M ia ilK
C ontents........................... Sum m ary..................................... .................................
lit....**..,.a.*.
.2
Develop and Produce a C-8 Alternative..................
.4attkltiti*
A dm inistrative ******!*****#***
Com m ercialize Fluoroproducts M ade Without C-8
4
******%5
Adm inistrative.... High Solids T E -3313 with FS-62 TA 1998 FS -62TA Needs
....5
*.** 'O5h ........ 6
Dispersion (PTFE) FE P ..
........7
...... 8
PFA
........ 9
P S -62 Supply Issues FE P Tuning...............
.**
FEP Serhworks Testing.............
........ 9
...........10
11
F S -62 Regulatory Issues............
M anage Existing C-8 Products and Processes.
Adm inistrative......... ............... .................... .
Dordrecht W orks C-8 Project S tatus..... ........ W ashington W orks C-8 Projects.....................
13
15
....................I.15
..1 5
17
Recovered C -8 Production................................
18
Testing of Recovered C-8
........... 18
W W C -8 A ir & Surface sampling update.......
........... 19
Industrial hygiene review of Jennifer Nichols C-8 sampling study by Playtis.......... 19
Concerns about personnel exposure on B-162 roof a re a ........................................... 20
Concerns about personnel exposure in the bead facility............................................. 22
M iscellaneous
**>*23
Steering Team
.....
a***.**..*.............23
Adm inistrative....
Risk analysis update........................
Environmental Degradation of C -8
23 **. ** 24
24..........................................
3M Issues........................................... FEP T im in g ....................................... IP P
24..........................................
2 4MtMIMIHt
..*..***...*.*24
II. B U SIN ESS O P P O W W T Y AND S TR A TE G Y ..
Path Forward
Appendix - C -8 Sampling Results..................................
......................
25
N9.Vf*i
***** 28
S um m ary
.
3 batches of T E -3313 grade PTFE dispersion were produced at 50% solids using FS62. Th e batches ran well with good reaction that was 10-15 minutes shorter than normal batches due to the higher initiator level producing standard m aterial but with an R pPS on the low side of the specification.
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January 1998
Significant plant tests (TA ) with FS-62 will be required in 1998 to m eet the commercialization schedule. In PTFE dispersion, a 7-10 batch campaign of the highsolids T E -3313 recipe is needed in 6/98. The material would be finished in a variety of products (G -108, T -3 0 ,3 0 B , 313, etc.). Finishes would like to see a concurrent production of F E P and PFA dispersion batches using F S -62 along with the G -108 so they can quality ail together as a system. This supports the long term strategy of moving all dispersion products to a single polymerization recipe. Timing for the Fibers conversion (33S ) Is uncertain due to continued problems with their new spin matrix. The most important FEP test is the 14 batch TEFLO N 5100 campaign scheduled for
3/98. Line 3 will require an ~ 10 batch campaign in 9 /98 after the line starts up. For dispersion, a single batch o f a G -1818 type recipe needs to be made around 6/98 to coincide with the G -108 test. This will be followed by T E -9519, G -493, and FEP 121 (each single batches). David G reene reported after the meeting that the 3/98 date for TEFLO N 5100 is highly unlikely due to supply issues. Finishes will need a batch of PF 350 grade dispersion around 6/98 to qualify with the G -108. A PFA 3 40 grade dispersion fo r powder coating would follow around 9/98.
The PTFE TA consumed virtually all FS -62 at Washington W orks. A raw material account for F S -62 which has been established, and an order 4,000 lb of25% FS -62 is being placed, l i t e next order will be need early 3Q 98.
A campaign of F E P Line 3 batches using FS -62 was completed in the semiworks to
explore FS -62 concentration, K N 0 3 loading, and purified F S -62. Two campaigns of
FEP dispersion fo r Ctrcleville (TE -9519) and Finishes (G -1818) were also run which
established the M FR shift between C-8 and FS-62 batches to allow adjustment to the initiator schedule and showed that FS -62 can be used down to 60% of the C-8 level.
National chemical inventory issues must be satisfied before making or sailing any polymer in th particular country. In the U S , FS-62 Is TS C A listed. In Japan, some of the componente o f F S -62 are listed, and Specialty Chem icals regulatory personnel will insure that it is satisfactorily listed. Specialty Chemicals is also working on the EINECS listing of FS-62 fo r Europe.
Food contact requirem ents apply to only some end uses, but DuPont has traditionally
not restricted any of the fluorocarbon resins from food contact. In the US (FD A 21 CFR
177.1550 Fluorocarbon articles & coatings), PTFE has already gone through extraction
testing, but FEP has not. A low molecular weight, high comonomer resin such as
TEFLO N 5100 will be used as "worst case" and with tests for both dispersion and
cube form. FD A testing will be conducted by an outside lab and take a few (3-6)
months. The Japanese'equivalent (Food Sanitation Law no-. 233 & JHOSPA) will be
easy to obtain after FDA approval since it recognizes FD A qualification. The European
requirements (Fram ework Directive 89/109/E E C ) are much more stringent and tim e
*
. consuming than FD A since FS -62 is not on a positive list. Cost and timing for Europe is
uncertain but estim ated at $30QM to $500M and requiring multiple (three to five) years.
The Dordrecht W orks dust eliminator appears to be functioning correctly after it was
modified to increase spray and then cleaned. Dordrecht has noted that Dyneon virgin
C-8 is w ater white while 3M , Miteni, and Dyneon recovered C -8 all have some
yellowish cast. T h e source and impact are being investigated
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January 1998
Both th e first and second step of the W ashington W orks Reverse Osmosis System have been operating well fo r the past 3 -4 months (since th e October shutdown). This is attributed to decreased w ax pluggage in th e first stage and a very low pH (3-4) making
calcium mom soluble in th e second stage.
W ashington W orks has several C -8 reduction projects in progress. The Pine Powder
Scrubber Filter Is authorized fo r a 6/98 startup. Both of the FEP scrubbers were
modified to allow fresh w ater to more spray nozzles which has increased C-8 recovery,
and further improvements are expected once the w ater flow can be increased. Initial
samples of the P FA scrubber shows that it is only 53-65% efficient A COO similar to
F IR 'S to increase w ater flows to reach design removal rates is in progress which is
expected to allow >90% C -8 recovery efficiency. A filtration facility for the FEP Effluent Carbon Adsorbers w as authorized as part o f package 6 in 12/97 for a 8/98 startup
(coincident with F E P line 3 startup).
The quantity o f C -8 recovered (20% ) h as grown frorriT 1M lb lri 1992 to T30M Tb in 1997
with a projection of 225M lb in 1998.
Both unpurified recovered C -8 from W ashington W orks and recovered C-8 from
Shimizu W orks purified by 3M w ere tested in a TEFLO N 5100 recipe in the
W ashington W ort semiworks with little difference from the C-8 standard.
Industrial hygiene concerns over C-8 air sam ple results at Washington Works are
discussed in th e m eeting note text. Actions are being taken in the B -162 roof area and
the bead facility.
.
3M completed file analysis of the sam ples looking for decomposition products of C -8.
The written report w as disappointing in th at it omitted reference to the most likely
decomposition products (C7F15H), and th e test accuracy was also low er than that
reported by outside laboratories. Dave Ellis is analyzing th e data.
3M visited W ashington W orks on Decem ber 8 and 9 to cover routine supplier relations.
At this tim e, they presented a "business as usual" picture and tried to reassure DuPont that they would be able to m eet our supply needs. Specialty Chem icals continues to
see signs that 3M is shorting customers.
Develop and ProduceaC^SA
A d m in istrative
The next m eeting will be held a t 8:00 am on March 4 ,1 9 9 8 , via an audio conference between the Experim ental Station 328/221 (originator), and Washington W orks B21 downstairs conference room (863-3615). Cham bers W orks can be included if desired. Topics fo rtiie next meeting w ill include:
FS -62 impurities and purification Update on alternative surfactant scouting
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January 1998
Com mercialize Fluoroproducts Mad W ithout C-8
Administrative
The January 7 m eeting w as attended by Bill Buxton, Bob Cavanaugh, Greg Chapman, and Leo Lech. T h e m eeting agenda is shown below.
Commercialize Pluocaoroducts Made W ithout C-8
The meeting w ill be held a t 1:00 pro on January 7 , 1998 in CRP 702-1242 {contact is Koenings) w ith an audio connection to MW (B21 Downstairs Small CR 8 883-3615, contact is Chapman).
Time
Topic
Leader
1:00-1:05 1:05-1:20
1:20-1:40 1:40-1:55
1:55-2:00
opening
Chapman
PTFE TA's w ith FS-62
- December high so lid s TE-3313te s t w ith FS-62 Lech
- Future te s t schedule
Chapman
- FS-62 needs
Chapman
Update on Regulatory TestingNeeds
Buxton
FEP Issues
Chapman
-P la n t Tests
-L in e 3
-Semiworks FEP Line 3
-Semiworks FEP Dispersion
Path forw ard items
Chapman
The next m eeting will be held at 1:00 pm on February 4 ,1 9 9 8 in CRP 702-1242 (contact is Koenings) with an audio connection to W W (B21 Downstairs Small @ 863 3615, contact is Chapm an). Topics for the next meeting will include:
TSL evaluation of Decem ber high solids T E -3313 test with FS-62 - Cavanaugh FEP Semiworks Testing - Line 3 recipe -C hapm an FEP Semiworks Testing - Dispersion - Chapman Update on TA schedule for FS-62 - Chapman
See path forward list at the end of this note for a list of all path forward items, responsible individual, completion dates, and status.
High Solids TE-3313 with FS-62 TA
Leo Lech reported that TA T -4687 had successfully produced 3 batches of TE -3313
grade PTFE dispersion at 50% solids using FS -62. The TA had some initial problems
with interlocks that caused two aborted batches. Th e software dumps the surfactant
tank when the batch aborts, and so this TA used up virtually all of the FS-62 at
Washington W orks.
.
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January 1998
The batches ran w ell with good reaction profiles and a 55-60 minute reaction tim e. This is 10-15 m inutes shorter than normal batches due to the higher initiator level. The raw dispersion had standard properties although the RDPS was a little on the low side. Leo felt the R D P S could be raised by adjusting the recipe. The conductivity was slightly elevated versus normal TE-3313 but sim ilar to high solids 0 8 batches.
The area Is engaged in a mini-PHA to allow a perm anent change to the weigh tank interlocks which w ill allow routine production of high solids batches. This is expected to be in place within three to six months.
TA T- 4687 50% Solids TE-3313 with FS-62
Fine Powder T A Schedule
Goals: Increase solids to 50% and replace C-S with FS-62
Two aborted batches due to software/interlock issues Three batches successfully produced
Consumed virtually all FS-62 at W W
The reaction profiles look good.
The raw dispersion quality was standard
=> RDPS w as on the low end of the spec.
=> Can be im proved through future recipe adjustments
First two batches concentrated per standard procedure.
W ent as expected
.
=> In spec fo r pH and solids
Third batch (double concentration) had problems with concentration
=> Insufficient Triton => Easy to correct
1998 FS-62 TA Needs
1998 will be a tim e o f increased testing of m aterial made with FS-62, and the test calendar will be full as illustrated by the following chart. Due to Finishes' need to qualify . systems which include P TFE , FEP, and PFA dispersion, w e will need to schedule tests in all three areas a t approxim ately the sam e tim e (6/98).
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|i 94 2Q94 3CJ9* 4Q94 1095 2B5 s o s ir 4^95 la u ti ZQB613Q96 4096 1Q97 2087 3097 4097 109812099 3U98 4098
PTFE Dfe ti 6*108 333 TE-3313
FEP Cub =gf>100 TEFS100 Llne3
1
1
- t" 1 .....
11
1"-------- 1----- -
1 1 1
7
FEP D is i G-493 TE-9519
1 1 I1
-- h-
" 4"
3 F-10 4 25%
14
4
10
1 1
1
FEP129
i
P FA D ie P PFA 340 PFA 350
Id fronj TE-3.113 baite red ........ r i t r : " T = i
------- i1-------
i i
1
1 1 I I
1
Dispersion (PTFE)
The next logical step in the PTFE dispersion conversion is to do a 7-10 batch campaign
of the high-solids T E -3313 recipe in 6/98. The material would be finished in a variety of
products (6 -1 0 8 , T -3 0 ,3 0 B , 313, etc.). Finishes would like to see a concurrent
production of FEP and PFA dispersion batches using FS -62 along with the 6 -1 0 8 so
they can qualify all together as a system.
'
The long term strategy would be to move all dispersion products to a single polymerization recipe. This would probably be built off of the high solids TE-3313 with FS-62. Timing for the Fibers conversion (33S ) is uncertain due to continued problems witti their new spin matrix. They will be making an ~1 M lb run in late January with T -30 and then a full scale prototype run in March. Conversion to an recipe that uses FS-62 will not be considered until after the spin matrix issues are solved.
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Proposed PTFE Dispersion TA Schedule for 1998
G -108 Single batch in 2Q98
Single batch in 4Q 98 Need to coordinate with FEP and PFA dispersion
Try to move towards using high solids TE-3313 base recipe
TE-3313 (combined with high solids work)
7-10 batches in 6/98 finished as: - G-108 - T-30 - 30B - 313
Begin commercial production (25% of sales) in 4Q98
33^ Assuming spin matrix is solved, 3 batches in 9/98 Try to move towards using high solids TE-3313 base recipe
FEP
'
The most important test is th e 14 batch TEFLO N 5100 campaign scheduled for 3/9 8 .
Line 3 will require an -1 0 batch campaign in 9/98 after the line starts up. For dispersion, a single batch of a G -1818 type recipe needs to be made around 6/98 to coincide with the G -108 test. This wilt be followed by T E -9519, G -493, and FEP 121 (each single batches). David G reene reported after the m eeting that the 3/98 date for TEFLO N 5100 is highly unlikely due to supply issues (see FEP Timing on page 10).
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Proposed FEP TA Schedule for 1998
t e f l o n 51 nn
14 batch campaign 3/98 (assumes 5 days of inventory) Un0 3
10 batch campaign 9/98 FEP 121 Single batch in 11/98 H r .9 5 1 9 (C jrcleville Dispareinn) Single batch in 9/98 0 -4 9 3 Single batch in 10/98 G -1 8 1 8 fo r equivalent)
Single batch in 6/98 coordinated with G-108 TA
FS-62 Supply issues on the
l E T " ? v"1ua,ly a" Fs'62 * " 08 " aed ^ " 98 --
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January 1998
FS-62 Needs
'a? -5*62 Inventory TE-3313 TA consumed virtually all FS-62 at W W . Only a few gallons in R&D and some heels in the FEP TBSA addition tank. Raw material account (021073) set up at Washington Works for FS-62.
Will order 1000 lb (A! basis) this week which will meet needs until 9/98
Next FS-62 order early 3Q98
FS -62 Needs Identification
Family Date
Semiworks
All
5 1 0 0 -1 4 batch campaign
FEP
TE-3313 -1 0 batch campaign (includes G-108)
PTFE
G-1818
FEP
PFA 350 Disp (for Finishes)
PFA
FEP Line3 - 1 0 batch campaign FEP
TE-9519 (Circleville Disp)
FEP
TE-3313 - 3-5 batch campaign PTFE (to be finished as 33-S & G-108)
G-493
FEP
FEP 121
FEP
PFA 340 Disp (for Finishes)
PFA
TE-3313 Commercial Production PTFE
-
3/98 6/98
6/98 6/98 9/98 9/98 2H98
10/98 11/98 4Q98 4Q98
FS-62 Required (lb Al basis) 5 Ib/month 300 lb 200 lb
60 lb 50 lb 200 lb 60 lb 1001b
60 lb 601b 501b 500 lb
FEP Timing
Greg Chapman covered th e semiworks batches. See FEP Semiworks Testing on page 11.
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January 1998
David G reene reported that the 14 batch campaign of TEFLO N 5100 with FS-62 on the existing lines which had been delayed until March 1998 will probably be delayed even further due to the supply situation. The criteria for the test is to have at least a five day supply of 51 0 0 going into a polykettle cleaning. H e did not see any problem in fitting dispersion tests in before any polykettle cleaning._________ __________ ________
*" --
FEP Timing
~
Plant Tests - Line 1 & 2 14 batches of TEFLON 5100 Supply is a critical issue
s=> Needs to be sellable material = * Precondition of 5 days supply of TEFLO N 5100
Next window is March 1998 TMA in draft form Line 3 Parallel qualification after start up Chapman to do COD so existing TBSA addition facilities can be tied into
Line 3
FEP Semiworks Testing .
Greg Chapm an completed a campaign of FEP Line 3 batches using FS-62. These were a duplicate of the recipes used by Aten for a wire line run except fo r surfactant.
The tests explored FS-62 concentration, K N 0 3 loading, and purified FS -62. The
batches ran w ell. Batch tim e w as slightly longer and M FR higher, but these can be corrected with m inor recipe changes. Th ere were slight differences in copolymer content but these can be explained by batch tim e. The RDPS with FS -62 was also smaller. Greg is doing additional work to understand how to increase RDPS.
Greg als o completed two campaigns of FE P dispersion for Circlevilfe (TE-9519) and Finishes (6 -1 8 1 8 ). He will finish and send to Mort Katz and Pete Huesmann
respectively. During the cam paign, he w as able to establish the M FR shift between C-8 .
. and FS -62 batches to allow adjustment to the initiator schedule. He also noted a difference in laser RDPS m easurem ents between R&D and the release lab. He was
able to run F S -62 down to 60% of the C -8 level.
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Semiworks F E P samples
Line 3 batches complete
Recipe * Duplicate of Aten's recipes exceptfor the use of FS-62insteadof C-8 =9 5 batches at varying FS-62 level (30% to 70% of C-8 level) 9 3 batches at 50% of 0 8 level withothermodfflcation
=> FS-62 purified using
(1) NH*OH and HNOaand noadded KNOa (2) KOHand HNOj and no added KNOa 9 50% OB levelwith additional KNOa
All except for30% of C-8 level had reasonable coagulum
Rate was slightly slowerthan C-8 =9 123-175 minutes for FS-62 vs. 113 -133 minutesfor the 0 8 batches inAten's
campaign
0*22 L-RDPS was lower than C-8 (0.14 micron avg. vs. 0.18 micron)
MFR higher
=9 Consistentwith other FS-62 runs
9 Easy to correct with modified initiatorschedule
. MWDI slightly higher
. Slight differences in copolymer incorporation
=9 Slightly lowerHFP Incorporation 99 Slightly higher PEVE Incorporation
*
TE-9S19 batches complete (2 cam paigns)
Recipe ` ' .... ..
...........
- => 33% solids (3500 lb batch)
=9 Pressure control with a non-linear (1.5 exponent) profile
First campaign showed: =9 Semiworks requires higher C-8 level '
= There is an MFR shift fromC-B to FS-62
=9 Slightly high HFPI L-RDPS difference betweenplant lab and R&D
-
Second campaign showed: =9 Can predict MFR shiftfromC-8 to FS-62 s> FS-62 can be run atabout60% of C-8 level
=> Split addition doesnothelp =9 Uke C-8, FS-62 will require an Increase In QPU to go to highersolds
=> 7 RDPS
G1818
Polymerized and ready to formulate based on "current"G-1818 (3500 lb batch with pressure control)
Wilt rerun in semiworks once plant recipe is finalized
............... ....................
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January 1998
\I
FS-62 Regulatory Issues
Bill Buxton reported on the issues surrounding regulatory approval of polymer made with FS-62. H e separated the discussion between national chemical inventory issues and food contact and covered the US, Japan, and Europe for each
National chemical inventory issues must be satisfied before making or selling any polymer In the particular country. In the U S , FS -62 Is T S C A listed, in Japan, some of the components of FS -62 are listed, but there is some uncertainty about w hether FS-62 ^
which is a mixture of isomers, acid, and NH4 salts is covered. Bob Buck will work with '
Specialty Chem icals regulatory personnel to insure that it is satisfactorily listed. Specialty Chem icals Is working on the E IN E C S listing of FS-62 for Europe.
Food contact requirem ents apply to only som e end uses, but DuPont has traditionally not restricted any of the fluorocarbon resins from food contact. In the US (FD A 21 CFR 177.1550 Fluorocarbon articles & coatings), PTFE has already gone through extraction testing, but FEP has not. Buxton recommends using a low molecular weight, high
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January 1998
comonomer resin such as TEFLO N 5100 as "worst case" and testing both dispersion and cube form (flake is not needed as it is no worse than dispersion and not use in large volum es). FDA testing will be conducted by an outside t o and take a few (3-6) months. The Japanese equivalent (Food Sanitation Law no. 233 & JHOSPA) will be easy to obtain after FDA approval since it recognizes FDA qualification. The European requirements (Fram ework Directive 89/109/E E C ) are much more stringent and time consuming than FD A since FS -62 is not on a positive list. Buxton recommends assembling a dossier after FDA extraction completed. Cost and timing fo r Europe is uncertain but estim ated at $300M to $500M and requiring multiple (three to five) years.
Regulatory Status of FS-62
'
(as of December 1997)
National Chemical inventories:
USA: TS C A - clear for commercial use (SPEC filed F S -62 reaction mixture).
Japan: M IT I - not clear Nagato Fujil (DKK) reports only two F S -62 ingredients of are registered. Kavsy Dastur (SPEC ) says others not registered. (request SPEC to file).
Europe: E IN E C S - not clear (requested S P E C to file).
Food Contact Status:
US: FD A 21 C F R 177.1550 Fluorocarbon articles & coatings verify low m olecular weight T P E /H FP /P E V E copolymer (like 5100 resin and dispersion) will m eet regulation. (submit four sets 150 sq. in. samples for extraction testing by outside t o per regulation).
Japan: Food Sanitation Law no. 233 & JH O SPA (standards) JHO SPA approval can be based on F D A qualification. (file with JH O SPA after FDA qualification).
Europe: Framework Directive 8 9/109/E E C F S -62 is not on positive list. (consider assembling dossier, after FD A extraction completed).
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January 1998
Manage Existing C -8 Products and P r o c e s s e s
Administrative The January 8 ,1 9 9 8 meeting was attended by Rik Brandenburg, Greg Chapman, John Migiiore, Jack Offenberger, Rob Pinchot, Tony Playtis and Roger Zipfel. The meeting agenda was:
Mannas E xistin a C-8 Products anrtProcesses
The meeting w ill be held a t 8:00 am on January 8, 1998 in CRP 702-1242 (contact is Pinchot) w ith an audio connection to WM (B21 Downstairs Small CR i 883-3615, contact is Chapman) and Rik Brandenburg a t DW
(347-1648)
Time
Topic
Leader
8:00-8:06 8:05-8:20 8:20-8:35 8:35-8:40 8:40-8:55
8:55-9:00
Opening DM C-8 P ro je c t Status & Learnings MM C-8 P ro je c t Status & Learnings
Recovered C-8 Testing J e n n ife r N ichols Study - Report back on previous studies - Issues w ith moving smoking area - S tatus o f to do items Path forw ard items
-
Chapman Brandenburg Z ip fe l Z ip fe l
P laytis Offenburger Chapman Chapman
The next meeting will be held on February 5 ,1 9 9 8 , at 8:00 am via audio conference between CRP 702-1242 (contact is Pinchot), W W (B21 Downstairs Small @ 863-3615, contact is Chapm an), and Rik Brandenburg's office (947-1648).
Topics for the next meeting will include:
Dordrecht W orks C -8 Prelect Status - Brandenburg Washington W orks C -8 Project Status - Zipfel Testing of DW recovered C -8 - Zipfel
See the path forward list at end of this note for a list of all outstanding path forward items, responsible individuals, completion dates, and status.
Dordrecht Works C-8 Project Status
Rik Brandenburg reported that the Dordrecht W orks dust eliminator was found to be plugged (high pressure drop) due to inhomogeneous w ater spray in which only the front candles were getting a full spray. Extra sprays were added so each of the 12 candles was sprayed by two nozzles, but the pressure drop was still too high after the shutdown due to blinding from prior operations. Dordrecht W orks developed a special in-place
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rinsing procedure which appears to have solved the problem with six days o f stable
X operation,
^ Rik also reported that Dyneon virgin C-8 has always been w ater white while 3M and Miteni product has som e yellowish cast to ft. The Dyneon recovered C-8 from FEP also
show some of the sam e yellow c a s t Rik and Roger Zipfel will work to identify the color form er and determ ine if this helps us understand if this might impact our ability to m ake ultra-high m olecular weight homopolymers.
Rik also discussed concerns about toe im pact that FS -62 might have on FEP H H T oven
rate to light o f recent capacity programs and C-8 recovery efforts. Greg Chapman
reported that a 14 batch TA is scheduled fo r TEFLO N 5100 at Washington W orks in March. This test should provide solid data on to e advantages and disadvantages in the process (including H H T rate). F S -62 will probably not be as much of a H H T penalty as TBSA w as; however, he tois ft is important to get the data from the plant test before drawing any conclusions either way. The issue is probably not as imminent at Dordrecht W orks as at W ashington W orks due to regulatory (particularly food contact) Issues which will probably take three to Five years. Greg also reported that FS -62 w as also being driven not just as a S H E issue but also from a cost and supply standpoint in
PEP.
H ie blood sam ples from TE FLO N homopolymers E shift is being analyzed for C -8.
Duplicates have been sent to the U S for a cross check. These results will determine if
additional shifts need to be sam pled.
DORDRECHT ITEMS
DW ITEM2: YELLOW DISCOLORATION IN C-8
1.
Z 3.
WORSNIMPSOTEOFCCUFLDWOHSPEUUTVRARSTCEIECNIUDTONSRGNIESNOCUNENUNBA(TTIVRNBPMIOIEFEAGRFEYDRCGSSARYIDT-IST<NOEAUUiY2LPABSRP.LILNTENROEDSEOFWBLAERBOILDPELMRRICEJSIU6EMONCSAADVOSTDTEALAIFYORYONIEREISRDNDDRAA,,E)PITTIMNLNIO1SAIL2SECN5ISDGEImI:ONH1mNTC-8
3M AND MTTENIVIRGIN: YELLOW DYNEON VIRGIN: WATERWHITE - DYNEON R-C8 FROM FEP: YELLOW JNAMP.ANESE SUGGESTTESTING AT400 DMYONLEEOCNULVAIRRGWINEIGGOHOTDRFEOSIRNSHIGH
. DDusWt EITlimEMina1t:or
* -
dpfoilsuutgnrigdbeucdatiiuonsneSeinphteommboegre1n9e9o7us(4s0p0ramymwaWteCr )
* addedindividual sprays for each candle
* still high dP after annual shutdown
* special in-place rinsing ofeach candle
* dPseems stable at appr. 125 mm WC
FEP OVENDCWAPITAECMITSY VS FS-62
FHOHRT5O1V00E-NN.ALREADYLIMITING WSOILOLNBE LIMITED FOROTHERTYPES FS-62 AGGRAVATESPROBLEM C-8 REMOVALPROGRAMS INFEP LESS JUSTIFICATIONTOUSEFS-62 IN FEP.
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C-8 PACE Team Meetings
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January 1998
' Washington Works C-8 Projects
a ,/ Roger Zipfel reported that the No. 2 Reverse Osmosis System has been operating well for the past 3 -4 months (since the October shutdown) when previous life was often only a few weeks. The pH has been very low (3-4) making calcium more soluble. He is
investigating increasing the surface area of the 2nd stage and evaluating alternative
m em branes.
The Washington W orks No. 1 Reverse Osmosis (RO) unit has also been operating well
with 6 months of continuous operation without any problems due to wax pluggage. One
section is being analyzed to better understand the w ax build up. A small COD is planned to add deep-bed filtration to remove wax from the Fine Powder scrubber.
Basic data and authorization are complete for the Fine Powder Scrubber Filter. The design is similar to the Dordrecht Works filter, and it will be reviewed by Dordrecht
W orks. Startup is scheduled for 6/98. This will reduce C -8 emissions by 12M Ib/yr,
Both of the FEP scrubbers have been modified (12/97) to allow fresh w ater to more spray nozzles. This was in response to TA learnings. Th e unit is currently water flow
limited, but the change has increased C-8 recovery, and further improvements are
expected once the w ater flow can be increased.
Initial samples of the PFA sorubber shows that it is only 53-65% efficient. A COD to increase w ater flows to reach design removal rates is in progress. This is similar to the modifications to the FEP scrubbers mentioned above, but it was slowed down to February 1998 based on cash conservation. The modifications are expected to allow
>90% C-8 recovery efficiency.
The FE P Effluent Carbon Adsorbers are currently off line due to high solids in effluent / waters. The filtration facility design is complete and w as authorized as part of package
6 in 12/97. ft has a projected 8/98 startup (coincident with FEP line 3 startup). The
scope Involves a one segm ent automatic pressure filter with filter aid (calcined rice hulls) that will also modify the pH to >5. The filter aid will result in a waste volume of -1 0 0 M Ib/yr to the landfill that is <10% FEP.
W W C-8 Recovery Status
ReverseOsmosisConcentration Status
Fine PowderScrubberFiller
- * Authorized 12/97
- * Start-up6/98
'
FEPScrubbers
- * Modificationsmade 12/97
- * Efficiency improved- data in lab
PFAScrubber
- * Initial samples showefficiency as 53-65%
- Modifications scheduled2/98
FEP E ffluent Solids Removal
Basic Data Complete Authorization -12/97 Scope
-- * ANueetodPfirletessruaride Filter Start-up 8/98
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C-8 PACE Team Meetings
-18-
January 1998
Recovered C-8 Production
Roger Zipfel presented the following chart which shows the increase in recovered C-8 volumes. The quantity of C -8 recovered (20% ) has grown from 11M lb in 1992 to 130M
lb in 1997 with a projection of 22SM lb in 1998.
Recovered C-8 Production H story Pounds Recovered per year
250000
1998B<p
200000
150000
; "
'S 100000 1 v
-...'ft.'- V-' ^ -=
)
i 50000
o
CL
0
II
1932 1930 1934 1995 1996 1997 1998
Testing o f Recovered C-8 Roger Zipfel reported that both unpurified recovered C-8 from Washington Works an d . recovered C -8 from Shimizu Works purified by 3M were tested in a TEFLO N 5100 recipe in the W ashington W orks semiworks. All values looked fairly standard except for some of the comonomer incorporation results which seem ed slightly low but might just be normal process variability. The unpurified recovered C -8 will be tested again when the Dordrecht W orks recovered C-8 purified by Dyneon arrives.
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-19-
Januaiy 1998
anwwteitesviteMF E terts;W
fchNQ
fttitie -rrih Gtegitm-gars MR-1 MRS MRS yITeHn
RTSnfaOB
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m-WB m m r m-mm m-W9
Grid bSm m K B O T F KBSBCBQ7
1 w w 139
eao m
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2292
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0191 Q1E0 0186 0181
OK om 098 030
vite vite vite vite
00 00 -nM4i 139 143 138
SB 80 m 89
WW 0 8 A ir & Surface sampling update
This section covers three topics:
1. Industrial hygiene review of Jennifer Nichols C-8 sampling study by Piaytis
2 . Concerns about personnel exposure on B-162 roof area 3 . Concerns about personnel exposure in the bead facility. Both a ir and wipe sample results are in the appendix at the end of this note.
Industrial hygiene review of Jennifer Nichols C-8 sampling study by Piaytis
Tony Piaytis reported on the Jennifer Nichols C-8 eampUng results study. The purpose of the program was to answer questions raised by the 1996 analysis of C -8 jobs which
was prompted by the 1995 blood data. A secondary purpose w as to do wipe sampling
as requested by Fran Mulherin & John Migliore. Most of this sampling w as in locations *
not included in the routine industrial hygiene monitoring program, since w e were looking
for previously overlooked routes of C-8 exposure. Most blood levels measured in 1995
were explainable by known job exposures. Two exceptions were: 1) Granular
polykettle operators (too high), and 2) FP dryer operators (too low).
Tony reported the following key observations:
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-20-
January 1998
* W ipe Sam ples - Com parable to 1980's results. Higher in Homopolymers than In
Copolymers, due to prevailing winds. Higher on surfaces that are undisturbed.
Higher indoors, since the roof gets cleaned by weather. Might explain granular
polykettle operator blood levels. Might be significant fraction of allowable daily dose
of 100 ug, but this is speculation.
.
* Control Room Samples - Usually very low, but with infrequent high spikes. Granular polykettle control room has higher spikes. M ight be significant, but need more data.
* Roof Samples - Air filters on HVAC systems do important work. Smoking area could be a problem.
H e saw the following continuous improvement opportunities for 1997-98:
Filters on C-8 exhaust.
W ork rules for the W ax Room and Bead Dryer Room.
Improvements in fine powder dryers.
Smoking area closure.
Additional follow-up monitoring.
Concerns about personnel exposure on B-162 roof area
The group then discussed the path forward items from the study (see the following chart for current status). The key point of discussion was personnel exposure on the B162 roof area. Tony Playtis agreed to run the B-162 roof sam ples through LOGAN, but with that many samples above th e action limit, he felt we will need to take action (i.e. move the smoking area). In addition, with the PPE requirements fo r construction
workers around the C -8 scrubber, there was concern that w e should investigate
whether an administrative procedure Is required around roof access in general. This area is used by FP/Dispersion, Granular, and monomer operators on a routine basis, and so it becom es a BTO issue rather than just one area. The proposed course of action was:
1. Playtis runs existing sam ples through LOGAN and recommends whether any action is required.
2. If action is required, Mattson will convene appropriate personnel to investigate roof access, moving smoking area, etc. Playtis will be the subject m atter expert, but decision on how to im plem ent (relocate smoking area, lim it access tim e through administrative procedure, change PPE requirements, etc.) becomes an operations
. issue.
After the m eeting, Tony ran the samples through Logan and m ade the following report:
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January 1998
INTEROFFICE MEMORANDUM
D a te : From:
Dept: T e l No:
0S-Jan-1998 02:19pm ANTHONY J . [TONY] PLAYTIS PLAYTIS
POLYMERS SHE&EA 304-863-2228
TO: Gregory A Chapman
CC: Roger J . Z ip fe l CC: ROBERT F, PINCHOT CC: JACK OFFENBERGER CC: ROBERT R. MATTSON
( CHAPMAGA )
( ZIPFEL ) ( PINCHORF ) ( OFFENBJL ) ( MATTSORR )
su b ject: RE: C-8 Exposure on B-162 Roof
I ran LOGAN and got the fo llo w in g pronouncement from the computer:
THIS EXPOSURE ASSESSMENT REQUIRES THAT MORE SAMPLES BE TAKEN. Continue sam pling, add the new data to th is data and rerun LOGAN.'
I ' l l ta lk to Becky about g e ttin g th is done. Meanwhile, the lim ite d amount o f tim e th a t someone spends in the smoking area can serve as an inform al a d m in is tra tiv e c o n tro l.
As to th e question o f general ro o f access, my understanding is th a t rooftop work is in fre q u e n t and not o f long d u ra tio n . I f th ere are exceptions to th is , o r i f th e re is any nonroutine work th a t w ill in vo lve long tim es on th e ro o f, we need to examine those situ a tio n s in d iv id u a lly and decide what to do, ju s t as was done w ith th e exhaust f i l t e r p ro je c t. However, i f th e BTO p re fe rs to sim ply req u ire a re s p ira to r fo r any rooftop stay lo n g er th a t a h a lf hour, th a t would be fin e too._________________
Based on these results, the course of action will be to take additional samples and hold off on any m ajor changes to adm inistrative policy until the data warrants it.
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January 1998
Path forward from C -8 Sampling at Washington Works |
Item ....
Responsible completion status
nrflvtdual Date
I
Comments
1 lataanalvslsofNtehete1C-8 samuraisprated
ibvbIod formatlordataentry ..........
... 3AC
4mmdata entered
3RM
AnatyzaOata
SAC
9/16/S7IComotete
mam Qraulato
w s t& t Complete
Stepchangedown on7/30197-See 10/97PACE
meettio notes
. LO
4087
Jomoiete
a ReduceC-BexnosurariskItem Granularingredientshood...
knntsmentshort-termmeasures(fixleak, ete.1
1ST
tmotamentiww-tamimeasuresfeurffectantatfoSHonsystem) RJZ
' 4WoifcwithHailavtomava 8162 2ndfloorsmokingarea
w
s installfitteronFPdryer0 8 vent
RJZ
4QS7 4098
n Progress InProgress Javetoolnoscope
1QSB
Retd Heedaddltianalairsamples
May-98
Basic datacomplete Prelect Authorized
6 InsurepropermafritenancaIsperformedanFP diyerasnoted SeaWrite Up
infnciefentfnvesUaatkmPDL970015
................
7 SotstandardIntheBTO to notwearclothescontaminated RRM withdisaeialonforother0 8 containingmaterials)...... ...._
1Q98
8 Resolveexposurepotential associatedwithdrainingot FP JL0/R5 ' 3098 htandtank4 coaofilters (automatedvalve?) ..............
9 InsureproperPPEla usedforchangingairfitterswith emphasisontheroofof B162.
JLD
Tracked throughCAR
Addto outfitform.
AmyBrownsettingupteam
Complete CurrantPPE acceptable. Rootcausewfil beaddressedby FP drver titter (Item 6)
10 MenaceC-Bexoosure ootentlal InvidnltvofOBscnibber UnderstandOS exposurepotentialon8162roof& surroundingareas
RJZ
4Q98
Instituteappropriate administrativecontrols.&PPE
RRMrfU2i 1Q9B
Takaadditional airsarnpleatocompletemapping
AJP/BSD *
Complete Rootcausewill beaddressed by FP dryer filter (Item 6) PPErequirementsfor constructiondetermined
Hold Construction complete Operations- waitingadditional
air samolno NotNeeded Rootcausewffl beaddressedby
FP drvarfUter (Item 51
11 CompareNichols'datawithpreviousdata (particularlyblood AJP
data) and took lorcorrelations
..............
IP Takewloasamples In FEPdean room.
............. BSD
13 tfC-8 Isgdngtocorrtinuatobe usedinPEP,Investigate ByLoch
enoineerinacontrolson C-8 levels.
............ ..
14 Evaluate Nichols'data and recommendadditional sampling BSD needs
Dec*97 complete See 1/93 PACEmeeting notes
1 Dec-98 Complete See 1/98PACEmeetingnotes
4QS8
Mold TSDafterFS-82tests
Dec-91 Complete AdditionalB162 toolsamples nearsmokingarea onlydries needed
Concerns about personnel exposure In the bead facility.
The bead oven room had an area sam ple result of 47.86 mpb while the ovens were
operating (AEL is 0 .S6 mpb). D ue to this high reading, Becky Szacket Dines retrieved
all of the 1997 results from bead. This showed other area samples in the sam e area of 0.96 mpb and 0 .8 3 mpb. All personal sam ples (4) were below the control lim it (0.13, 0 .0 2 ,0 .1 8 , and 0 .0 8 m pb). This Is a controlled area where operators are not permitted in the room w hile the ovens are operating. The frequency of sampling has been
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increased from 90 days to 3 0 days, but no other changes have been made. The team agreed that this w as the appropriate action.
Miscellaneous
John Migliore mentioned that Power and Services at Washington W orks has decided against using th e old Lubeck wells for process and domestic water; therefore, there is
no concern about treatm ent for the low but detectable levels of C-8 in the w ater.
Steering Team.
Administrative
The January 8 ,1 9 9 8 m eeting was attended by Bob Buck, Bill Buxton, Greg Chapman, M att Koenings, Steve Korzeniowski, Rob Pinchot and Roger Zipfel. The meeting
agenda was:
___ _____________________________
S teering Team
The meeting w ill be held on January 8 , 1998 a t 1:00 pm v ia audio conference between CRP 702-1242 (o rig in a tin g s ite ) and Washington Works 821 downstairs conference room (863-3615), O ther s ite s need to provide a phone number to M att Koenings.
Time
Topic
Leader
1:00-1:05 1:05-1:15 1 :1 5 -1 :20
Opening Update on Sub-team meetings
R isk an alysis update
1:20-1:25 FEP Timing 1:25-1:30 --Environm ental Degradation o f c-8
1:30-1:35 3M issues
1:35-1:40 FS-62 Issues
- Order
- EINECS L is tin g
1:40-1:55 Prep fo r IPP
1:55-2:00 Path forw ard items
Chapman Chapman Kennedy Chapman ,Z ip fe l A ll
Chapman Buck Chapman Chapman
The next meeting will be held on February 5 ,1 9 9 8 , at 1:00 pm via audio conference between C R P 702-1242 (originating site), W ashington W orks B21 downstairs conference room (863-3615). Topics for the next m eeting will include:
Risk Analysis Update - Kennedy . * Regulatory status of F S -62 - Buck
FEP FS -62 Timing - Greene/Chapm an
See the path forward list at end of this note for a list of all outstanding path forward items, responsible individuals, completion dates, and status.
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Risk analysis update
No report.
Environmental Degradation o f C-8 .
Roger Zipfel reported that 3M had sent us a report on the analysis of the samples
looking fo r decomposition products of C -8. T h e written report omitted referenceto the most likely decomposition products (C 7F 15H ), but verbal communications had indicated
that there w ere no decomposition products. Their reported test accuracy is also lower than that reported by outside laboratories. Roger wilt follow up with 3M to get written confirmation o f the level of decomposition products and understand why their analytical methods w ere not more sensitive.
Dave Ellis analyzed the data, and it indicates that C-8 is disappearing faster than the
current understanding of w ater flow. H e is revising the model at this tim e.
3M Issues
Greg Chapm an reported that 3M visited W ashington W orks on Decem ber 8 and 9 to
cover routine supplier relations. At this tim e, they presented a "business as usual" picture and tried to reassure DuPont that they would be able to m eet our supply needs. Matt Koenings reported the assurances o f continued supply w as probably due to our having forced them to do this to m eet our contract. At this m eeting, 3M handed Roger Zipfel a copy o f his low toxicity FS -62 patent signaling that they were aware of our work
in this arena.
.
Steve Korzeniowskl and Bob Buck reported that Specialty Chemicals continues to see signs th at 3M is shorting customers. Bob indicated that 3M is also shorting perfluorcarbon customers and increasing prices on these product and indicated that we
should keep Peter Chen aw are of 3M activities.
FEP Timing See FEP Timing on page 5.
IPP
The team discussed responsibility for the IP P . Greg will coordinate and write the report and have responsibility for sections I, IV , and V . Matt has already provided input on section II. Roger will help with section III.
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January 1998
Prep for IPP
S c h e d u le
jf Phase II R eview /IPP on Feb. 6
Issue IPP 1/30
First Draft 1/12
_____ _
Initial Input by 1 /5 TM f . BCECUTIVE SUMMARY
es
Commercial Manufacturing Overview Program Schedule And Staffing and Resources
Financial Summary Major Issues, Risks, Impacts And Assumptions , Deviations from PA C E Guidelines //. BUSINESS OPPORTUNITY AND STRATEGY
A . Opportunity Definition & Program Fit B. Competitive Overview C . M arket and Product Strategy D . Technology and Production Strategy
PRODUCT^r S S eSS SPECIFICATION SUMfc
,.. Product/Process Description And Application
B. Summary O f Key Product Goals C . M ajor Technical Risks A r JI A* s--su"mptions IV. PROGRAM SCHEDUU STAFFING &
A . Program Plan Overview
B. Core Team Diagram C . Detailed Program Plans fo r N ext Phase
TEC H N O LO G Y: Technical Service TEC H N O LO G Y: Research & Development, Plant Technical
M ANUFA C TU R IN G /O PER A TIO N S
M ARKETING: Product Group
M ARKETING: Marketing & Development
SALES D . Project Capital Resource Requirements
E. Phase III Schedule
V. FINANCIAL SUMMARY
,, ^ iV
A. Financial Param eters(See Financial Model Input Sheet)
B. Cash Row and Earning Statem ent Financial Spreadsheet Analysis
C . Document Assumptions Used For Analyses_______________ ,______
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Path Forward
Item
Responsible
D evelop and Produce a 0 8 A lternative
C om m ercialize Fluoroproducts M ade W ithout 0 8
Develop test to determine residual surfactant as a function of time, temperature, and thickness. Apply to FS-62
Titrate H4-C8 batch to see if any of the surfactant is lost during polymerization.
Understand the lot to lot variability of FS-62 andwhich tots were used for each sample.
Make TE-9519 with FS-62 forevaluation at Clrdeville
Evaluate FS-62 based G559 with and without post addedsurfactant.
Produce G1818 with FS-62 in the semiworks
Begin dialog with Gore on T-30 made with an alternate surfactant
Outline testing for regulatory approval of polymermade with FS62 in US and Europe.
Review 5100 TMA using FS-62
Evaluate FEP inventory and determine when toe 5100 TA using FS-62 can be run
Chapman
Treat
Treat/Zipiel
Chapman Huesmann/ Cavanaugh/ Chapman Chapman Fernandes
Buxton -
Buxton Greene/FEP S&OP
M anage E xisting C -8 Products and Processes
Schedule industrial hygiene review for Shimizu Works
Update CEP to refled FEP carbon absorbers notcoming on line until 7/98.
Discuss with WW water team not using old Lubeck wells for domestic water without propertreatment
Pinchot Zipfei
MigBore
Date
6/97 6/97 7/97 7/97
7/97 12/97 11/97 12/97 3/97?
4098 1/98 1/98
StetoS
Hold Drop No findings Complete see notes See notes See notes See notes
Timing changed to 4Q98 Not being pursued
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C-8 PACE Team Meetings
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January 1998
Identify colorformerthat is not in Dyneon virginC-8
Note on reviewing C-8 exposure on B-162 roof
Run B162 roof C-8 air samples through LOGAN Convene groupto implementappropriateactionsaround B-162 roof C-8 air samples
Steering Team Determine patent strategy for FS-62low toxicity in fluoropolymerization
Brandenburg/ZipfeJ Chapman Playtis Mattson
3/98 1/98 1/98 Hold
Koenings,
10/97
Korzeniowski, Tocker
Determine if 3M will share technofogyon recovered C-8
Chapman
purification ifthey are not interested tncontinuing to purify C-8.
1/98
Get written confirmation of the level of decomposition products from 3M and understand why their analytical methodswere not more sensitive.
Zipfel
2/98
Complete Complete - Continue sampling Waiting on additional C-8 sampling results
Koenings spokewith Klmpel, and their is no current business driver to exploit the patent at this time.
Maritee Maendler (3M) needs to checkpatent issues before any furtiier discussions.
SttOZOZfH
0 8 PACE Team Meetings
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January 1998
Appendix - O S Sam pling Results
Poston
Sample# Payroll# Date Result Wind/ Morning Wind/ Afternoon Weather Root (mpb)
F iP Oven Control Boom, Position2
(TCP231)
N. Offices Root HVAC
(TMQ045)
Bead Oven Room
TCP603
FEP Oven Contml Room, Position 1
(TCP231)
FP&D AutoctavaContml Room Intake
(TM04S)
FP FinishingDryerOperator
(TTF1028PI)
Wax RoomHVAC Hake
(TM0045)
Wax RoomHVAC Intake
(TMO045)
Granular PolykettiaContml Room
(TTF060)
GranularPolykettieControl Room
(TTF060)
FEP Oven Contml Room, Position2 Wax RoomHVAC Intake
(TCP231) (TMO045)
Wax RoomHVAC Intake
(TMO04S)
Betid OvanRoom FP&DAutoclaveControl Room Intake
CP63 (TMO04S)
FP&D AutoclaveControl Room Intake
(TMO45)
Bead Oven Room
TCP603
FP Finishing (Dryer) Control Room
(TTF031)
Wax Room HVAC Intake
(TtoMS)
Wax Room FP&D AutoclaveControl Room Intake
(TTp028) (TMO045)
FEP Polykettie Control Room, Position t (TCP2l)
FEP ExtruderControl Room
(TCP26B)
MonomerControl RoomHVAC Intake
(TMO045)
B162 2nd Level OutsideSmoking Area
(TMQ048)
Wax Roam
(TTF02B)
Wax Room Wax Room
(nF028) (TTF028)
Wax Room
(TTF02B)
MonomerControl Room HVAC Intake
(TMO04S)
#3 Slab DropWhile In Use
(TCP237)
Wax Room
(TTF028)
wax Room
(TTF028)
MonomerControl RoomHVAC Intake
(TMO045)
FP FinishingtOiyar) Control Room
(TTF031)
B1622nd LevelOutside SmokingArea
(TMCKMS)
FP&D Autoclave Control Room Hake
(TM004S)
FEP Polykettls Control Room, Position 1 ..(TCP21S)
Wax Room
(TTF028)
B162 2nd Level Outside SmokingArea
(TM0048)
FP Finishing Dryer Operator
(TTF102/Q8PI)
Wax RoomHVAC Intake
(TMO045)
#3 Slab DropWhile In Use
(TCP237)
FEP OvenControl Room, Position 2
(TCP231)
B162 2nd Level Outside Smoking Area
(TMO048)
4872 4382
08107/97 Spilled 07/10/97 Spilled 10/21/97 47.88 07/17/97 4,31 07/25/97 2.90 07/14/97 2.43 07/29/97 2.17 07/24/97 2.13 07/09/97 1.91
maam 1.80
07/18/97 1.69 07/22/97 1.21 07/23/97 1.08 03/27/98 0.96
marni o is
07/29/97 0.94 07/09/97 0.83 07/21/97 0.76 07/2S/97 0.69 07/23/97 0.52 07/23/97 0.51 08/04/97 0.48 07/28/97 0.45 07/29/97 0.45
miasm 0.43
07/24/97 0.43 07/21/97 0.42 08/04/97 0.41 07/11/97 0.40 07/24/97 0.39 07/28/97 0.37 07/10/97 0.37 07/25/97 0.36 07/25/97 0.34 07/23/97 0.33 07/11/97 0.32 08/05/97 0,30 07/29/97 0.29 07/22/97 0.20 07/10/97 0.26 07/25/97 0.26 07/21/97 0.26 08/08/97 0.25 07/29/97 0.25 07/25/97 0.23
S NNE S SW
NE NE 3E
SN SS E NWS SN NE NE SW w
3s sN
NE NE
sE 3w 3w
3 SSE N " NS s. N E NW 8S NE NE 3 SSE 33 SS
S SW SE 3E SW S3 SSE SSE 3N SW NWS 3 SW
NS NE
SN s
Clear Clear Y
Clear Cloudy
Clear Y Rain Y Rato Clear Clear Cloudy Y Cloudy Y
Rato Clear
Clear Cloudy Y Cloudy Cloudy Stormy Cloudy Clear Y
Rato Y Rain Clear Stormy Clear Rato Y
Clear Cloudy Cloudy Y Ctoudy Clear Y
Clear %
Clear Cloudy Clear Y
Clear Y
Clear Cloudy Y
EID092895
RJZ020736
E ID 092895
C-8 PACE Team Meetings
29
January 1998
@1622nd Lave!OutsideSmoWngArea
(TMO048)
FEP Oven Control Room, Pssition2
... (TCP231)
FEP PolykettleControl Room, Position 1 (TCP215)
81622nd LevelOutsideSmokingArea ... (TM0048)
iOffioasRoolHVAC
(TMO045)
=EPOven Control Room, Position 1
(TCP231)
rPSO AutoclaveControl RoomMaim WaxRoom HVAC Intake
(TM0045) (JM0045)
07/23/97 08/08/87 08/07/97 07/24/97 07/25/97 07/28/97 07/22/97 08/05/97
0.23
0.23 o .a 0.22 0.22 0.19 0.19 0.19
loadoven Room =EPOven Control Room, Position 2
TCP603/18PJ Contract 03/27/97 0.18
(TCP231)
07/14/97 0.18
FP Finishing Dry Operator B1622nd LevelOutsideSmokingArea FEPOven Control Room, Position 1 MonomerControl RoomHVAC Intake ?EPOven Control Room, Position 2
(TTF102/D8PIT (TMO048)
(te m i) (TMO045) (TCP231)
4824
07/25/97 07/21/97 07/29/97 07/22/97 07/18/97
0.18 .17 0.17 0.17 0.16
FPFinishing DryerOperator MonomerControl RnomklVAC intake
(TTF102W8PI) 10203 08/06/97 0.18
(TMQ045)
m a r n i 0.16
@1622nd LevelOutsldasmoking Area
(TMO048)...
m a r n i 0.15
N. Offices RoofHVAC p/8 FEP E&l Mach/ Shutdown N. Offices RoofHVAC Bead Oven Room MonomerControl Room N.Offices RoofHVAC A/S PEP Slab Racks C-8 RecoveryOperator FEP Oven Control Room. Position 1
(TMQ045) COPOLYMERS
(TMO045) TCP803M8PJ
(TMO100) " " (TMOMS) COPOLYMERS (TTFOS8/O0PM)
(TCP231)
1019
7/2/97 ' 9/97*11/# ' 0.15 07/24/97 0.14 07/11/97 0.13 08/05/97 0.13 O7/ I I /97 0.3 9/97-11/97 0.12 07/17/97 0.12 07/30/97 0.12
FEP Polykettle Control Room. Position2 CTCP21S)
08/04/87" 0.12
FP Finishing (Dryer) Control Room
(ffF M )
m a r n i 0.11
GranularPolykettle Control Room
. (TTFOS)
- 07/11/97 0.11
MonomerControl RoomHVAC Intake
(T04S)
m a r n i 0.11
N. Offices Roof HVAC N. Offices Roof HVAC FEP Oven Control Room. Position 1
CTMO045) (TM0046) (TCP231)
m a rn i
07/09/97 07/14/97
0.11 0.10 0.09
A/S 2 InitiatorPlatform
COPOLYMERS
9/97-11/97 0.08
BeadOven Room
TCP603/18PJ Contract 07/09/97 0.08
FEP Oven Control Room, Position 2
(TCP231)
07/17/97 0.08
FP Finishing (Dryer) Control Room
(TTF031)
07/25/97 0.08
FEP Oven Control Room, Position i
(TCP231)
07/18/97 0.07
FEP Oven Control Room. Position 2
(TCP231)
07/31/97 0.07
FEP Oven Control Room, Posidon 2
... (TCP231)
m a r n i 0.07
MonomerControl Roomhvac Intake
(TMOD4S)
08/05/97 0.07
N.Offices Root HVAC
(TMO04S)
07/22/97 0.07
B182 2nd Level Outside SmokingArea
(TMO048)
08/07/87 0.B
C-8 Recovery Operator
(TTF088/08PM)
08/05/97 0.06
FEP Oven Control Room, Position 1 FP Finishing (Dryer) Control Room
crcpai)
(TTF031)
0718/97 0.06
07/11/97 006
FP Finishing DryerOperator
(TTF102/08PI) 10214 08/12/97 0.06
FP Finishing DryerOperator
(TTF102/08PI) 10177 08/06/97 0.06
Wax Room
(TTF028)
07/09? 0.06
S
ssw s s s
N
sw
SSE
NE
NE S SW NE
S SW NE
S
SSE 8
NE S S
s s
NE 3 E N
NE S NE S N SSE SW S SSE NE S
E
EED092896
W SW NNE
S E MS NWS SSE
N
NE N NWS E
w
NWS NE
s
SSE S
NE SSW SSE SSW
S NE W NW NE
NE E E NNW NS SSE NWS NNE SSE NE S
NW
Cloudy / Clear Clear Rain Cloudy Y Cloudy Cloudy Clear Y
Clear
Clear Y Clear Cloudy Y . Clear
Cloudy Y Cloudy Y Clear Y
Rain Y
Clear !-
Clear Y
Clear Clear Stormy Clear Sear Clear Y Cloudy Y Rain Y Clear
Clear Cloudy Clear Clear Cloudy Clear Y Cloudy Y* Clear Y Clear Clear Clear
(tain
RJZ020737
EID 092896
RJZ020738
i
0 8 PAPE Team Meetings
30
January 1998
B isa 2nd LevelOutsideSmokingArea FOP ExtruderControl Room FEP Oven Control Room, Position 1 REP PolyketllBControlRoom, Position 1
(TMO048) (TCP268) (ICFZ31) (TCP215)
08/04/97 07/14/97
m m fflr
07/14/97
0.05 0.0S 0.05 0X5
s NE S NE
FP Fintshing(Dryer) ControlRoom
(TTF031)
07/24/97 0.05
8
FPSD Autseteve Control Room MOnomarControl Room
(TTF010) (TMOIOO)
07/11/97 0.05 07/28/97 0X5
8 N
PEP ExtruderControl Room
(TGP268)
07/18/97 0.04
NE
FEP ExtruderControl Room
(TGP28B)
07/17/97 0X4
NE
ra p ExtruderControl Room FEP Oven Control Room, Position i PEP PolyfcetHeControlRoom, Position 2
(TCP268) (TCP231) (TCP216)
08/07/97 07/31/97
0.04 0X4 0X4
NE S s
PP Finishing (Diyer) Control Room FP&D Autoclave Control Room New FEFControtRoom New FEP Control Room P/S FEP FK Operator FP dwenControl Room, Position 1 ' FEP Oven Control Room. Position 2 raP PolyfcetHeControl Room, Position2 FP Finishing(Dryer) Control Room
(TTP031) (TTF010) (TCF28Q) (TCP280) COPOLYMERS (TGP231) (TCP231) (TCP218) (TTF031)
08/07/97 0.04
rnasIsT 0.04
07/28/97 0.04 07/17/97 0X4 9/97-11/97 0.04 07/31/97 bxa ' ' 08/04/97 0.03 07/29/97 0.03 08/06/97 0.03
S S N NE
S s s s
NewPEP Control Room
(TCP280)
07/14/97 0,03.
NE
P/S DayPolyAreaMechanfc
Homopolymers
8/97-11/97 0.03
P/ FlnePowderOryarOp
Homapotymers
9/97-11/97 0.03
P/s Shift Mechanic
' MONOMER
0/97-11/97 0.03
A/S#2 BoosterPump Bead OvenRoom
COPOLYMERS
$97-11/97 0.02'
TCP603/18PJ Contract 07/13/97 0.02
Bead Ovan Room
TCP611/18PJ Contract 04/08/97 0.02
Bead Sweeco Screener FEP Oven Control Room, Position 1 F^P OvenControl Room, Position 2
TCPQ10/18PJ i&ntract 07/09/97
(TCP231)
08/04/97
(TCP231)
08/08/97
0.02 0.02 0.02
S s
PP Finishing (Dryer) Control Room FP&D Autoclave Control Room FP&D Autoclave Control Room
(TTF031) (TTF01) (TTF01)
07/22/97 08/07/97 07/24/97
0.02 0.02 0.02
sw
s 's
PP&D Autoclave Control Room MonomerControl Room
(TTF010) (TM0100)
07/23/97 0.02 07/25/97 0.02
s s
MonomerControl Room
(TMOIOO)
07/23/97 0.02
s
NewFEP Control Room
(TCP280)
07/16/97 0.02
NE
P/S FEP General Day Mach
COPOLYMERS
9/97-11/97 0.02
PIS FEP General Day Mech
COPOLYMERS
9/97-11/97 0.02
P/S FEP Genera) Shift Mech
COPOLYMERS
9/97-11/97 0.02
Bead LaserInspection
TCt611/18PJ Contract 03/27/97 0.01
Bead Oven Room FEP Polyketiie Control Room, Position 1 FEP Polyketiie Control Room, Position 2
TCP611 (TCP215) (TCF215)
03/27/97 08/08/97 07/30/97
0.01 0.01 0.01
ssw s
FEP Polykettle Control Room. Position 2 (TCP21S)
07/18/97 0.01
NE
FEP Poiykele Control Room, Position 2 (TCP21S)
07/17/97 a o i
NE
FP Finishing (Dryer) Control Room
(TTF031)
07/10/97 ao i
s
FP&D Autoclave Control Room
(TTF010)
07/28/97 0X1
N
MonomerControl Room
(TMOIOO)
07/29/97 0.01
S
SSE Stormy
NE Clear
SSE Clear
NE Sear
S Rain
S Clear
NS Cloudy
NE Sear
NE Sear
E _ --jg --
Sam Sear
NNW
Clear
NNE Sear
E Soudy
NS Cloudy
NE Sear
NNW SSE
N SSE NE
Sear Stormy Saar Sear Sear
SSE SSE NWS NNE
S W E W E
Stormy Clear Cloudy Sear 'Rain Cloudy Cloudy Cloudy dear
SW SSW NE NE SW NS
N
Sear Clear Clear Sear Sear Soudy Clear
B ID 092897
E ID 092897
0 -8 PACE Team Meetings
-31 -
January 1998
aw FEPControl Room aw FEPControl Room >m Dispersion Packout P/SFEPE5IMechanlo IS FEP GeneralShift Moon ead Oven Room ead OvenRoom /SDiyerControl Room A/S DryerControl Room 3 GranPKControt Room A/S WaxRoom 1622nd LavalOutside SmokingArea
(TCP280) (TCP28) -tomopolymers COPOLYMERS SOPOLYhfRS TCP611 TCP811 Komopotymera Homopolymers omopolymera iomopoiymers CTM048)
C-8 RecoveryOperator
(TTF06B/Q8PM)
>8 RecoveryOperator
(TTFD68/08PM)
FEP ExtruderControl Room :EP ExtruderControl Room
(TCP288) (TCP2B8)
FEP Extruder Control Room
(TCP268)
FEP ExtroderCentral Room
(JCP288)
FEP ExtnrderControl Room (TCP2S8)
F6P ExtruderControl Room
(TCP288)
FEP OvenControl Room. Position 1
(TCP231)
=EPOven Control Room. Position2
(TCP231)
PolyicatliftControl Room. Position 1 (TCP218)
=EPPotyketUeConirolRogm. PositionT (TCP25)
FEP PotyKettleControl Room, Position 1 (TOP215)
FEP Polykettle Control Room, Position 1 =EPPolykettleControl Room. Position 1
(TCP215) (TCP21S)
FEP Poiykettla Control Room, Position 1 (TC|P2S|
=EPPoiyketUeControl Room, Position 1 (TCP21S)
<EPPoiyketUeControl Room, Position 1 (TCPEsS
=EP PolyketHeControl Room, Position 1 (TCP215)
FEP PoiyketUeControl Room, Positron 2 FEP PoiyketUeControl Room, Position 2 :EP PoiyketUeControl Room, Position 2
(TCP215) (TCP21S) (TCP215)
FEPPoiyketUeControl Room, Position 2 (TCP215)
FEPPoiyketUeControl Room, Position2 (TCP215)
FEP PoiyketUeControl Room. Position 2 CTCP215)
FEP PoiyketUeControl Room, Position2 (TCP21S)
FEP PoiyketUeControl Room, Position 2 (TCP21B)
FP.RofsWng pryer) Control Room
(TTF031)
FP Finishing (Dryer)Control Room
(TTF031)
FP Finishing (Dryer) Control Room
(TTF031)
FP Finishing(Dryer) Control Room
(TTF031)
FP Finishing (Dryer) Control Room
(TTF031)
FP Finishing(Dryer) Control Roam
(TTF031)
FP Finishing (Dryer) Control Room
(TTF031)
FP FinishingDryerOperator
(TTF102/08PI)
FP Finishing DryerOperator
{TTF102/08^1)
FP FinishingDryerOperator
(TTF102/08PI)
FPftD AutoclaveControl Room
(TTF010)
07/30187 0.01 07/18/87 0.01
s .. SSW NE NE
3/97-11/87 0.01
8/97-11/97 0.01
9/97-11/87 0.01
04438/97 0.00
10/07/97 0.00
9/97-11/87 0.00
8/87-11/97 ado
9/97-11/97 0.00
9/97-11/97 OXO
07/30/97 0.00
3
08/08/97 0.00
ssw
07/08/87 0X0
ME
08/08/97 0.00
ssw
08/08/97 0.00
3
08/04/87" 0.00
8
07/31/87 0.00
S
07/30/97 0.00
3
07/29/87 0.00
3
"08/08/97 0.00
SSW
07/30/97 0.00 08/13/87 " T O "
3 s-
08/^2/87 aoo
3
08/06/97 0.00 ..... " 'V
07/31/87 aoo
3
07/30/97 0.00
S
07/28/87 aoo
N
07/18/97 0.00
NE
.. 07/17/97 0.00 " 51 07/16/97 0.00 ' 51
08/13/97 0.00
s
08/12/97 0.00
3
( m a m 0,00
3SW
08/07/97 0.00
S
08/06/87 0.00
3
07/28/97 oid
N
07/16/97 0.00 .... NE
07/14/97 0.00
NE
08/13/97 '"d io "
S
00/12/97 0.00 ....... SSE
08/08/97 0.00
sP?
08/03/97 0.0
SSE
08/04/97 0.00
S
07/31/87 0.00
S
07/09/97 0.00
E
SSW sw NE SW SSE SSE NNW SSW
N sw SSW SE SEE
SSE NNW SSW
NS NE NE E SE SEE SW NNE SSE NS
E NE SE E SW SSE SSE NNW NW
4382 08/12/97 0.00
4824 08/12/87 0.00
iooo 07/14/97 0.00
08/13/97 0.00
S
SE
EID092898
Clear Clear
Clear Y Clear Clear Clear Clear Stormy Clear Clear Clear Clear Clear Rain Rain Clear Clear " Clear Cloudy Clear Clear d e a r..
Rain Rain Clear Clear Clear Cloudy Clear Clear Rain Rain Clear Clear Stormy Clear Rain
Rain
RJZ020739
E ID O 9 2 8 9 8
C-8 PACE Team Meetings
-3 2 -
FP&D Autoclave Control Room FP&D Autoclave Control Room FP&D Autoclave Control Room FP&D AutodavsControl Room FP&D AutoclaveControl Room FP&DAutodavsControl Room FP&D AutodavsControl Room PPM}AutodavsControl Room FP&D AutodavsControl Room FP&DAutoclave Control Room GranularPolykattie Control Room GranularPolyketUeControl Room GranularPotyketdeControl Room GranularPofykatUsControl Room GranularPolykottleControl Room Granular FCtytcettle Control Room GranularPelykettJeControl Room Giaiiular Polykettte Control Room GranularPolykstao Control Room Granular Pclyksttls Control Room Granular PolykettteControl Room GranularPotykattlsControl Room Granular PolykottleControl Room GranularPolykettle Control Room GranularPolykettle Control Room MonomerControl Room MonomerControl Room MonomerControl Room Monomercontrol Room MonomerControl Room MonomerControl Room MonomerControl Room MonomerControl Room MonomerControl Room NewPEP Control Room NewFEP Control Room New FEP Control Room NewFEP control Room NewFEP Control Room NewFEP Control Room NewPEP Control Room NewFEP Control Room P/SC-8 Rec Op Chg Filters P/S bay Poly E&l Mechanic P/S FEP ExtruderOperator P/S FEP Flake PackoutOp P/S Fine PowderAC Op P/S Fins PowderPackout P/S Wet Finishing Operator
CTTF010) (TTF010) CTTF010) (TTF010)
CITF01Q) (TTF010) (TTF010) (TTFOIO) (TTF010)
PP3W "
fiTFOeO) (TTF060) (TTF060) (TTF06Q) (rrF060> {TTF060) CTTF060) CTTF060) (TTF060) (TTF060) (rrF060) (TTFQ60) CTTFOeO) (TTFOeoJ (FTF060) (TM0100) (TM0100) (TM0100) (TM0100) CTMOIOO).... CTM0100) (TM-iO) (TM0100) (tMOlOO) (TCP2B0) (TCP280) (fcP280) (TCP2B0) rrcpaeo) CTCP280) (TCP2S0) (Tcpaso) Homopolymers Homopoiymera COPOLYMERS COPOLYMERS Homopolymers Homopoiymera COPOLYMERS
January 1998
08/12/97 0.00
SSE
08/08/97 0.00
ssw
08/05/97 0.00
SSE
08/04/87 0.00
s
07/31/97 0.00
s
07/29/97 GOO
s
07/22/97 0.00
sw
07/21/97 0.00
NE
07/10/97 GOO
s
07/09/97 0.00
E
08/13/97 0.00
s
08/12/97 GOO
SSE
.08/08/97 0.00
ssw
08/07/97 GOO
s
08/05/97 0.00
SSE
08/04/87 0.00
s
07/31/9? 0.00 07 S F " goo"
S
N
07/25/97 GOO
s
074/97 0.00
s
07/23/87 0.00
s
T B S U r ] 0.00
07/21/97 0.00
NE
" W tS S F 0.00
s
07/08/07 0.00
N
08/13/97 0.00
s
o/ia/y 0.00
SSE
08/08/97 GOO .....ssw
08/07/97 0.00
s
08/04/97 ' w
s
07/31/97 GOO
s
Q7/24/97 0.00 07/22/97 0.00
s aw
0/2/97 0.00
NE
08/13/87 0,00
s
08/12/97 0.00 08/08/97 0.00
SSE
ssw
08/07/97 0.00
s
08/06/97 0X0
s
08/04/97 0.00
s
07/31/97 0.00
s
07/29/97 0X0
s
9/97-11/97 0.00
9/97*11/87 0.00
9/97-11/97 0.00
9/97-11/97 0.00
9/97-11/97 0.00
9/97-11/97 0.00
9/97-11/97 0.00
E Rain
sw si""
Clear Clear
SSE Stormy
NNW
Clear
N Clear
NWS
Cloudy
NE Clear
sw dear
NV? Rain
- gg-.... .
Rain
E Rain
SW Clear
NNE
Clear
" a r ~ Clear
SSE Stormy
NNW
Clear
Cloudy
E Cloudy
S Rain
W Cloudy
NWS
Cloudy
NE Clear
SW Clear
NE dear
SE Rain
E Rain
SW biear
NNE
dear
SSE Stormy
NNW
Clear
S
Uws
Rain Cloudy
NE Clear
SE Rain
Rain
SW Clear
NNE
Clear
SSE Clear
SSE Stormy
NNW
dear
N Clear
EID092899
RJZ020740
EID 092899
C-8 PACE Team Meetings
-33-
January 1998
Atea
j Location
oMretlta ControlRoom Area ... IHnmcpolyme(B1BZ) ID(rearArea
I iryimnnhfmnril ( IliB o fir lH a ti^ ly m e re {B ira |ayerAres
Is a re in a )
fe 1 fia te StoraneHowiar
H om opolytM tt{Bi62) i^R acove iy Contrai Room Area
H m iopotpw ralBiBZi otykattta Control Boom Atea
Sample Location
esult aurca
(U9)
4783 hito o ls
o ahM C ortrolR ocm alC teanR oom endofdryew ontop
painted Metal
S1102
to o ls
0 n re o o la ia a ia fli e n w a B te # B iitW a s v (8 !B iiiB f lata) ifcu rti# O w 8 ira w R p o ra (W a xlta < m B n d } im a ll hfatal
T2T7T1iSw? Ssends
11242 EKto o ls
nnaM sheflonlB O w arM fc
-
xM ajcca dw nw hia ta^hth aniidd ta of die entire area
la id fatal
ET arums
822 5SChots
m o riv fla t surfacethatwas d rtv
.....
smaflvihterefrigeratortoth left ofmixing hood by C-8 elatedMelal 77.4 llchots
1
-L'_____ _
"
roo of oven room hoodvent #3 oven )ven room welqh desk
.........-
..... fetal fe ta l
M.
70.1 Im lm ta Dinas 12118197Note
lls i E M I t |H tnop otyrnets(B 162)
| lopof monitor
Haste
822 UcholS
E T 3ra>cats Dines12/16/97 Note
liiilS
B
H F f f Clean Room
.........
Autoclave Control Room
on top o f king shelf thathas monlton! sitting on tt
M lhated Wood Haatic
4 8 3 SSuSs " ^ u r..
"ET Sjnkflte Dinas 12718/97Note
M23BaadFSeltitv K cm o |H ^m e i8 (8 i^ Fine Powder Finishing (Dryer)
nnM M lRm nt
Hcmopotymera(B1B2) diverArea
In Foremarfs room adjacentto monitorroom on lop ot cahiw t in rearcomar Dry Screen Room on blue switch boxes for moisture
Painted Metal 40.1 Nichols PaintedMetal 382 Nichols
Homopolytnera (B ieaT Warehouse HomopolynMra(B162) RootArea
analyser
~
behind fits pactoutdispersion area on ten supply camnet Painted Metal 31.1 Nichols
hv desk
. . . _______-- -------------------
m inside ledge o fn o th and of AC partol 8 Autoclave Metal
Control Room HVAC unit
...
29.7 Nkhols L-- ------------- -- -- -----
Homopotymera(BlB2) DryerArea
along westwan by#3 d y e r on top ofyellow breathing err Painted Metal 292 Nichols
box________
_
HomopoljmBfs(B162) Auloclava/Potyfcattte Conlrol Room on top o f tan filing cabitelroughly in-betweeneacft
Painted Metal 28.6 Nichols
Control Room
.......
Homopdymsrs(B162) ReelArea
o n b a sa d to b a cksilB (wax unittide) of IhaFPDryar area end da m kam derit hood axhmrst
Metal
283 Nlchofe
Homopofymars(B162T PackouUXspsralonArea
at sm dl controlpanel (across from Btalrwell doorway) on ClearPiasfc | 27 2 Nichols too o l face shieldbox
Homopdymera{B162) Women's Lounga
.
across to n doorto smoking area - on top o fmicrowave Plastic Covered
263 Nichols
FEP (B163) Areas
Warehouse
FEP (B163) Areas
Dispersion Packcut Area
Homoodvmers(B10Z) SmoldnaArea
FEP (B163) Areas
sw um*
tomoimivment(BlSE) O w anAftt
HomooelYmera<Blfi2) Autodava Control Room Bead Facilite BeadFacBtv
Homopolymers (B162) PolyketHe Control Room
.........
waralwusa along turnaround area - on top o f box lor
Painted Wood 267 Nichols
safMv masses herfde o fdoorbom turnaround area on lop of deswetotage stand In-between the Dbparsloo Metal
263 Nichols
Packout aad and wash bash
-- fe ta l
E T llchols
In-between Dispersion Pactout and Dry Flake Pactout Metal
253 Nichols
laadfori to second floor) on tadne haSwav upstate ------
bn t o d monitor a tta r and (from door) o f control panel
FEPO vens-tooofvellow m etal-#1 oven
......
o n todreM sam tor.........
-
A to retriqeratorln braakroom
...... .
on top of microwave
Plastic
'2 3 4
' 23.4
Painted Meta!I 232
Metal
` 222
Plastic
" 212
Covered
Nichols
.
Szakats Dinas 12/5/97 Note
ic h o ta
_
Szakats Dines 12/16/97 Note.
Nichols
FEP IB163) Areas
#3 Slab Oreo
Homopolymers (B162) N .Q fflcs*area
Homoootvmers (St62> Roof Area Homopolymets (B162) Lunchroom - MonomBr Control
jnsm aonsroauiecqatoren .....
Painted Meta T S 3
off o l confdorby MonomerControl Room * Iasioffice on Painted Meta 173
MUSafiffiu ti) on fiSno cafatot of desk
. .....
on anainoaB at oomm orw ax noom n w w iii # ' a Metal
" 16.4
on top of beige reWgaratw
Painted Metei 163
(Chois Nichols
Vkhols Nichols
re ..
Monomer Control Room
FEP (B163) Areas
Extruder Area
B-123 Bead Faddy FEP (B163) Areas
B e a d F a d liv Oven Area
on underside of the N. Offices HVAC Unit Wake
on top o fmonitot (undervent) in computet/monitof mom
adtacentta control area
.... _
on top o f lockers against the wall besH aoftheold
ExtruderControl Rocm
--
FEP O vens-too of exhaust-bav out #3
...
Metal H aste
" 153i Nichols ' 1531 Nichols
Painted Mato 15.<! Nichols'
Metal
" " w i Srekats Dines 12/16/97 Note I 1331 Szakats Dines 12/5/97 Note
EID092900
T I t A T A ^ r V T
E ID 092900
0 -8 PACE Team Meetings
* 34 -
Januaiy 1998
FEP 0 16 3 ) Areas
Extruder Area
onlop o f w hite exhaustve nt on HVAC u n it in southwest Painted M etal 1 33 Nichols com ero f area (to tfra side o f dooiw av to haiw av offices)
f f p m ie n Areas
*2 FS C lear) Room
Homopotymors (B162) Ron! Area
AtoD betthousfno
- Vletal
a t w estend o f Monom er C ontrol Room HVAC unit on top M etal
o f sm al box underneath o f lam er safety switch box
11.9 Szakats Dines 12(16197 Note 1 1 2 Nichols
FS>(B1E3) Areas
Sm okinaArea
R u ffA rea
1
reflected sefflcte o f d ust kr vent (wetohinq 0.09351 (jam s)
*
1 1 9 flch ols
s m a S b lo e b iK to id e ilM g e b U ^ to c iiw a a a ro tin d com er Painted M elal 9 9 Nichols
H m breatosoin a c o rn ft m stretcher
M. Tank Faffft H onpolvm ora(B182)
F E P (B 1 6 3 )A re a s = g (a i6 3 )A " rjP lB l8 3 t Areas FEP (8163) Areas
6ns Powder Packout Room MonomerC ontrol Room Oven A rea D rvFtJka Packout Area
Oven Area
Ovan Area
M.Tank F a rm -to o o f brealW no a ir sta te n
9 3 SzaJats Dines 12(5(97 Note
Com er ram o lin a # 3 D W itkn
................. dstal
9.9 Izakals Dinas X W W l Note
on too o fm onitor In midrSa o f controlnanel
3tasHc
8 .4
F E P O v e n s -to o o fe x h a u s t-# ti*2
8 3 Szakats Okies 12/5/97 Note
on too o lblack a ir m ask b ox a t braalhlnnalr s ta to r 18
3aktted Metal 8 2 Nichols
FEP O vans-olasttc s h ie ld -tra y o u t#3
8.0 Szakats Dines 12(5(97 Note
on top o l ok! O ven C ontrol Room AC u n i behind Control Painted Metal 7.8 Nichols
Room `n front o f convovorsvslam
Hanapolymere (8162) Hanooolvnwra (6182) H nu re a lvim is (8162) FEP (8 1 6 $ Areas
F ile Powder Packout R onn R na P onder Packout Room F its P onder P a c ta n Room Oven Area
Too o f P tadrfas w eloh station
Too o f control n a n e lln e #3
.......... T o o d r n B o lp a n e l& re # 2
................._
on topo f storage cabinets along back wag across from
Oven A3
"ta s te 3 M etal M otel
7 3 Szakats Dines 12(16197 Note 6 3 Szakats Okies 12(16(97 Note 6 9 Szakats Okies 12(16(97 Note 6 5 Nichols
FEP (0163) Areas
Second F loor Polykettle Control Room
a t fa r end (from door) o f contort area on top o f box th a t houses tw o m onftore
Lam inated W ood
B .t Nichols
FEP (8163) Areas
Oven A nte
on blue 'chock scale* panel box in-batvreen conveyor svstem and O ven #1
Pakrted M etal 4.7 Nichols
Hotnopotyttiars (B162) FEP (8 16 $ Areas
PotvkBtia C ontrol R o o m ................ on too o f black coat rack Inslda door
Painted M etal
O ven A rea
rm btoe booton w all In-between Oven 2 and the old Oven Painted M elal
C ontrol Room
45 44
Michels N ich o ls
ii
jn
Hanopotym aig (B162)
FEP (B163) Areas
Break Room
Too o f temrr/humd control box across from PolykeM e C ontrol Room - on top o f brovm vendim machine
M stal
4.S Szakats Dines 12(16/97 Note
Painted M etal 4.1 N ichols
FEP (6163) Areas
Oven A rea
on top o f breathing a ir station 31 black box h-betwaan Painted M elal 2 5 Nichols
Oven #2 and convBvor system
...... ` .................... . .
FEP IB1631 Areas N. Tank Farm M2 Homopotymera (8162)
New C ontrol Room Polyketde C ontrol Room
B-12 B-12 FEP (B163I Areas
Oven Area
an loo o f m onitor alonO dhrldtnd w all
N . Tank Farm - too o f m eter
B -12ofeeboN ndfiretruck8
doodmob,as you e nte r C ontrol Room (roughly 100em(2)
area)
............. ..
B-12 M . Botev's office on cabinet
B-12 too o f (lira cabinet
F B * O vens- to o o l cla s tic shield - # 1 4 #2
Plaster M etal
1 3 Nichols 1 5 Szakats Okies 12/5/97 Note 1.4 Szakats Dines 12/5/97 Note 1 .t Nichols
0.7 Szakats Okies 12/5/97 Note 0 5 Szakats Okies 12(5/97 Note 0 3 Szakats D ie s 12/5/97 Note
RJZ020742
EIDG92901
EXD092901