. £ UNITED STATES ENVIRONMENTAL PROTECTION AGENCY " WASHINGTON, D.C. 20460 OFFICE OF CHEMICAL SAFETY AND POLLUTION PREVENTION Lisa M Amadip Regulatory Affairs Manager Mason Chemical Company JUL 1 5 20l4 721 W.Algonquin RD Arlington Heights, IL 60005 SUBJECT: .Maquat TC76-10%-S - EPA Registration Number: 10324-15 Application Dated: April 16, 2014 Receipt Date: April 21,2014 Dear Ms. Amadio: This letter acknowledges receipt of the amendment identified above submitted under the Federal Insecticide, Fungicide, and Rodenticide Act (FIFRA), as amended. • Label revision: Alternate dilution rate for swimming pool instructions. Based on a review of the label and proposed changes submitted April 16, 2014 this amendment is acceptable. The changes to the label will be made part of the record for this file. Should you have any questions concerning this letter, please contact John Cowden at (703) 347- 0259. Sincerely, |*Velma Noble Product Manager (3 1) Regulatory Management Branch I Antimicrobials Division (751 OP)
Transcript
.£ UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
" WASHINGTON, D.C. 20460
OFFICE OF CHEMICAL SAFETYAND POLLUTION PREVENTION
Lisa M AmadipRegulatory Affairs ManagerMason Chemical Company JUL 1 5 20l4721 W.Algonquin RDArlington Heights, IL 60005
SUBJECT: .Maquat TC76-10%-S -EPA Registration Number: 10324-15Application Dated: April 16, 2014Receipt Date: April 21,2014
Dear Ms. Amadio:
This letter acknowledges receipt of the amendment identified above submitted under theFederal Insecticide, Fungicide, and Rodenticide Act (FIFRA), as amended.
• Label revision: Alternate dilution rate for swimming pool instructions.
Based on a review of the label and proposed changes submitted April 16, 2014 thisamendment is acceptable. The changes to the label will be made part of the record for this file.Should you have any questions concerning this letter, please contact John Cowden at (703) 347-0259.
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owev
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ts c
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hem
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clea
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ects
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ided
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hen
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fer
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acat
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se d
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ith m
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oves
filter o
pera
tion
and
redu
ces
need
for
othe
r ch
Q.in!c
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ct im
parts
tone
and
a p
leas
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rodu
ct i
s fo
rmul
ated
to
com
plem
ent
swim
min
g po
ol
wat
erch
lorin
e sy
stem
s.
It is
esp
ecia
lly e
ffect
ive
agai
nst
grow
th•la
tile,
ai
ds
in
mai
ntai
ning
po
ol
wat
er
clar
ity
and
spa
rene
ss o
f thi
s al
gaec
ide
tend
s to
sta
biliz
e th
e to
tal c
hem
ical
tn
Q-ro § •£en E ' °
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P °0.0
^
^ 5
~ °
TIV
AT
ION
: U
se
bent
onite
cl
ay
at t
he
min
imum
ra
tio
of 5
pp
m
c\i
;t. T
his
prod
uct
mus
t be
dea
ctiv
ated
prio
r to
dis
char
ge o
f th
e N
PD
Epl
y th
is p
rodu
ct m
ore
than
4 ti
mes
a y
ear.
0 3 0 -
2i 1-gQ Q. C
s$3q= £0 3LO 5£
^ 0 ,
O O CO
Subse
quent
Dose
: W
hen
mic
robi
al c
ontr
ol i
s ev
iden
t, ad
d 6.
4 1
ounc
es (
5 to
15
ppm
on
an a
ctiv
e qu
ater
nary
bas
is)
per
1000
gal
in t
he
syst
em t
wic
e w
eekl
y or
as
need
ed t
o m
aint
ain
con
trol
.
<3
syst
ems
mus
t be
cle
aned
bef
ore
trea
tmen
t is
beg
un.
rV
= >> a) ~ P >« CDi T> -Q £ E jo n
— Q- "D S f) in M~ ^
5 .8| - 8 o- ~s f -s8. fe^-°^ 1
ON
CE
TH
RO
UG
H F
RE
SH
AN
D S
EA
WA
TE
R C
OO
LIN
G S
YS
TE(N
ot ap
plica
ble
in C
alifo
rnia
.)osi
ng loca
tion:
Thi
s pr
oduc
t is
to
be a
pplie
d at
a p
oint
in t
he s
yste
me
unifo
rmly
mix
ed,
such
as
at th
e su
mp.
osi
ng c
onditi
ons:
T
his
prod
uct
mus
t be
app
lied
whe
n th
e s
yste
m i
f bei
ng a
ffect
ed o
r af
ter
clea
ning
sys
tem
s w
here
effi
cien
cy i
s al
read
y i
leth
od o
f applic
atio
ns:
. W
ear
safe
ty g
lass
es,
rubb
er g
love
s an
d im
perv
ious
apr
on.
. T
o re
duce
foa
min
g, m
ix 1
0 pa
rts
of w
ater
to 1
par
t of
this
pro
duct
.A
dd p
rodu
ct d
irect
ly f
rom
dru
m o
r ad
d th
e pr
oduc
t at
a p
oint
wh
mix
ed u
nifo
rmly
.U
se 0
.75
to 7
.5 fluid
ounc
es (
0.6
to 6
ppm
on
an a
ctiv
e qu
ater
nath
ousa
nd g
allo
ns.
Do
not
disc
harg
e w
ithou
t pe
rfor
min
g pr
oper
de
activ
atio
n.de
activ
atio
n us
e be
nton
ite c
lay.
The
min
imum
rat
io t
o be
use
d is
£to
5 p
pm o
f pro
duct
.D
o no
t us
e pr
oduc
t m
ore
than
4 t
imes
per
yea
r..
Tre
atm
ent t
ime
cann
ot e
xcee
d 12
0 ho
urs/
appl
icat
ion.
. A
void
oxi
dize
rs a
nd
redu
cing
ag
ents
. P
rodu
ct i
s ca
tioni
c an
dm
ixed
with
soa
p or
ani
onic
sur
fact
ants
.
1 _ I J D L J O « S T O - Q O "O CD >vJ O) -E:
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MO
DIF
IED
INTE
RM
ITTE
NT
ME
TH
OD
Initial
Dose
: W
hen
the
sys
tem
is
notic
eabl
y fo
uled
, ap
ply
12.8
ounc
es (
20 t
o 4
0 p
pm o
n a
n a
ctiv
e qu
ater
nary
bas
is)
per
500 g
alin
th
e sy
stem
. A
pply
ha
lf of
thi
s in
itial
do
se w
hen
half
of t
hesy
stem
has
bee
n lo
st b
y bl
owdo
wn.
Subse
quent
Dos
e:
Whe
n c
ontr
ol o
f m
icro
bial
gro
wth
is
evid
ent,
19.2
fluid
oun
ces
(5 t
o 15
ppm
on
an a
ctiv
e qu
ater
nary
bas
is)
per
of w
ater
in
the
syst
em.
App
ly h
alf
of t
his
subs
eque
nt d
ose
whe
wat
er in
the
sys
tem
has
bee
n lo
st b
y bl
owdo
wn.
Bad
ly f
oule
d sy
stcl
eane
d be
fore
tre
atm
ent
is b
egun
.CO
R;IN
TERM
ITTE
NT O
R SL
UG M
ETHO
DW
hen
this
tre
atm
ent
is r
equi
red,
add
thi
s pr
oduc
t at
the
rat
e of
ounc
es p
er 5
00 g
allo
ns o
f w
ater
alre
ady
in t
he s
yste
m,
or b
eing
syst
em,
for
4 to
8 h
ours
, 1
to 4
tim
es p
er w
eek
or a
s ne
eded
to
desi
red
leve
l of
con
trol.
Whe
n co
ntro
l is
obt
aine
d, a
dd t
his
prod
uof
6.4
to
19.2
oun
ces
per
1000
gal
lons
of w
ater
in t
he s
yste
m.
CO
NTIN
UO
US
FEED
ME
TH
OD
Initial
Dose
: W
hen t
he s
yste
m i
s no
ticea
bly
foul
ed,
appl
y 12.8
•Q U
E •*"o. Q-
TO
0 °
>- oCO Q
EA
CT
IVA
TE
: U
se b
ento
nite
cla
y at
the
min
imum
rat
io o
f 5
ppm
cct
. D
eact
ivat
ion
mus
t oc
cur
prio
r to
dis
char
ge o
f th
e N
PD
ES
out
fall,
•odu
ct m
ore
than
4 t
imes
a y
ear.
Q 3 Q.
00. «H Q.£
^ 00H( f-
— CD O
1 § §>
(20
ppm
on
an
ac
tive
quat
erna
ry
basi
s)
per
1000
ga
llons
of
syst
em.
Subse
quent
Dose
: M
aint
ain
this
tre
atm
ent
by s
tart
ing
a co
ntin
6.4
fluid
oun
ces
(5 p
pm o
n an
act
ive
quat
erna
ry b
asis
) pe
r 10C
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O
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? 2o Q: a
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— (— -4->(1) tt) m
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-Q ™ "§ £co ,_ £ t=
fic t
reat
men
t re
quire
men
ts v
ary
amon
g oi
l an
d/or
gas
fie
ld s
ites
anjn
ents
. T
he
Prim
ary
poin
t of
tre
atm
ent
will
va
ry
amon
g oi
l and/
tions
de
pend
ing
on
the
site
pr
oble
ms,
w
ater
-flo
od
trea
tmen
t rr
nent
. T
his
prod
uct
mus
t be
add
ed w
here
it
will
dis
pers
e ra
pidl
y an
dss
ired
area
of t
reat
men
t.
o Q- S Q- -S
C/) o O CD £
« "2m "5CD Q.
i 1 ;i
(Not
appl
icabl
e in
Cal
iforn
ia.)
osi
ng
Loca
tion:
Thi
s pr
oduc
t is
to
be a
pplie
d at
a p
oint
in
the
sys
II be
uni
form
ly m
ixed
/suc
h as
at t
he s
ump.
osi
ng C
onditi
ons:
T
his
prod
uct
mus
t be
app
lied
whe
n th
e s
yste
m i
bein
g af
fect
ed o
r af
ter
clea
ning
sys
tem
s w
here
effi
cacy
is a
lread
y im
Q S Q o
• CN
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^3 <D to13 m <"5= 5 O.
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a g|
eth
od
Of A
pplic
atio
ns:
INTE
RM
ITTE
NT
OR
SLU
G M
ETH
OD
Initi
al
Dose
: W
hen
the
sys
tem
is
notic
eabl
y fo
uled
, ap
ply
0.7J
ounc
es (
0.6
to 6
ppm
on
an a
ctiv
e qu
ater
nary
bas
is)
per
1,00
0 ga
lba
sed
on s
yste
m f
low
rat
es.
The
min
imum
tre
atm
ent
is 6
to
24 h
S ce
co
Hfo^gS
>, ^- C Q) • C T
IE -o^l I E^S5«?H!
fic t
reat
men
t re
quire
men
ts v
ary
amon
g oi
l an
d/or
gas
fie
ld s
ites
anjn
ents
. O
il fie
ld flu
ids
and
su
bsys
tem
s m
ost
com
mon
ly
requ
irini
natio
n co
ntro
l ar
e ra
w w
ater
sou
rces
, se
para
tors
, ba
llast
, st
orag
esc
reen
s,
surf
ace
inje
ctio
n eq
uipm
ent,
prod
uctio
n eq
uipm
ent
(suc
hro
duct
ion
pipi
ng
cast
ing,
co
mpl
etio
n an
d va
lvin
g)
and
the
form
atio
ry p
oint
of t
reat
men
t w
ill v
ary
amon
g oi
l an
d/or
gas
field
oper
atio
ns o
e pr
oble
ms,
wat
er-f
lood
tre
atm
ent
met
hods
and
equ
ipm
ent.
Thi
s pr
ocw
here
it
will
dis
pers
e ra
pidl
y an
d un
iform
ly t
o th
e de
sire
d ar
ea o
f tre
a
'o Q. ro co "• co -^ 5
W 8 8 S'ro o.£ ^
CU O ;o Jjj — O CD £
CO g* 5= S •£ CO "*"' S
o S S g S E E ' S -un
til
cont
rol
is a
chie
ved.
D
eact
ivat
ion
mus
t be
con
duct
ed
prio
rfr
om t
he s
yste
m b
y us
ing
bent
onite
cla
y at
a m
inim
um r
atio
of
51p
pm p
rodu
ct:
'S
ubse
quent
Dos
e:
Whe
n m
icro
bial
con
trol
is
evid
ent,
add
3/8
ounc
es (
0.3
to 3
ppm
on
an a
ctiv
e qu
ater
nary
bas
is)
per
1,00
0 ga
lba
sed
upon
sy
stem
flo
w
rate
s on
a
as
need
ed
basi
s to
m
air
Fre
quen
cy o
f fe
ed m
ust
be t
ied
to a
n in
-pla
nt m
onito
ring
prog
raco
wlin
g gr
owth
. D
eact
ivat
ion
mus
t be
con
duct
ed p
rior
to d
isch
asy
stem
by
usi
ng b
ento
nite
cla
y at
a m
inim
um
ratio
of
5 pp
m c
l
Q.
O
en
'5CD
flj
Q
2LEQ.
CD
£3
cu-Q
to
1
1j3"0o
CO
'oenco
<
"o•ooQ.
i
.22 .«L Oh- %
SrS|
nent
, su
ctio
n (lo
w p
ress
ure)
sid
e of
pum
ping
equ
ipm
ent
or s
imila
rct
can
be
adde
d to
the
sys
tem
by
slug
, co
ntin
uous
or
on a
n in
tern
ding
on
the
degr
ee o
f sys
tem
fou
nd.
o. = o5
CD Q.-D
° cr CO C c O }rCO E CO ~ 5 CM y "&
™§°° |
b.
INTE
RM
ITTE
NT
DO
SA
GE
Initi
al D
ose:
Whe
n th
e sy
stem
is
notic
eabl
y fo
uled
, ap
ply
76.7
5 ou
nces
ppm
act
ive
ingr
edie
nt)
of th
is p
rodu
ct p
er 1
000
gal
lons
of w
ater
in t
he s
yste
App
ly fo
r 3
to 8
hou
rs d
aily
unt
il co
ntro
l is
achi
eved
.M
aint
enan
ce D
ose:
Whe
n co
ntro
l of
mic
robi
al g
row
th i
s ev
iden
t, ap
ply
38ou
nces
(30
ppm
act
ive
ingr
edie
nt)
of th
is p
rodu
ct p
er 1
000
gallo
ns o
f wat
eth
e sy
stem
dai
ly o
r as
nee
ded
to m
aint
ain
cont
rol.
c.
CO
NTI
NU
OU
S F
EE
D M
ETH
OD
Initi
al
Dos
e: W
hen
the
syst
em i
s no
ticea
bly
foul
ed,
appl
y 20
oun
ces
(15
pac
tive
ingr
edie
nt)
of th
is p
rodu
ct p
er 1
000
gallo
ns o
f wat
er in
the
syst
em.
Sub
sequ
ent
Dos
e: M
aint
ain
this
tre
atm
ent b
y st
artin
g a
cont
inuo
us f
eed
oiou
nces
(15
ppm
act
ive
ingr
edie
nt)
of t
his
prod
uct
per
1000
gal
lons
of
wj
daily
or
as n
eede
d to
mai
ntai
n co
ntro
l.
AN
D G
AS
PR
OD
UC
TIO
N A
ND
TR
AN
SM
ISS
ION
PIP
ELI
NE
S A
ND
SY
STE
MS
i con
trol
of s
ulfa
te-r
educ
ing
bact
eria
and
slim
e fo
rmin
g ba
cter
ia,
this
pro
duct
mle
d at
a p
oint
in
the
prod
uctio
n or
tra
nsm
issi
on p
ipel
ine
via
dire
ct i
njec
tion
a'h
ere
unifo
rm.
The
appl
icat
ion
mus
t be
cond
ucte
d to
ens
ure
max
imum
dis
tribu
prod
uct
thro
ugh
the
inte
rnal
sur
face
of
the
pipe
line
by a
ddin
g an
am
oun
i whi
ch e
vent
ually
com
es o
ut th
e ot
her
end
of th
e pi
pelin
e. C
riter
ia f
or s
ucce
ssat
men
t w
ill b
e re
duct
ion
in b
acte
rial
coun
t an
d/or
cor
rosi
on r
ates
. To
fac
ilit
S cri 'i oci « ro £ic i — *" « -C-. O f P C O C D^ r--. 4= ^ — -~ -^ _.
M 5S§ ^ != m?2S 3^0 Sg % > £ < £m -0°,,. *^-c o°oP a j ^ > 30 Q j n o
>? f2" "g^ 1 t •§,n ^ ^ O C J2 C
O/L
RE
LD W
ATE
R F
LOO
D O
R S
ALT
WA
TER
DIS
PO
SA
LA
ND
FR
AC
TUR
ING
FLU
IDS
For
the
cont
rol
of s
lime
form
ing
and
sulfa
te r
educ
ing
bact
eria
inor
sal
t w
ater
dis
posa
l sy
stem
s, a
dd 5
-10
ppm
(ac
tive)
of
this
gallo
ns p
er 3
,000
bar
rels
of
wat
er)
cont
inuo
usly
. Le
vels
for
«va
ry d
epen
ding
on
cond
ition
s at
the
site
.Fo
r in
term
itten
t use
, do
se a
t ra
te o
f 5
- 20
ppm
(ac
tive)
of t
his
gallo
ns p
er 3
,000
bar
rels
of
wat
er)
for
4 to
8 h
ours
per
day,
wee
k as
nee
ded
to m
aint
ain
cont
rol.
For
treat
men
t of
flow
bac
k re
turn
wat
er (
Pos
t H
ydra
ulic
Fra
ctur
of 5
-20p
pm a
ctiv
e of
this
pro
duct
(4.
7 -
18.9
gal
lons
per
3,0
004
to 8
hou
rs p
er d
ay,
one
to f
our t
imes
a w
eek
as n
eede
d to
ma
«-' CN CO
!>
|£
'|
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~
OIL
FIE
LD IN
JEC
TIO
N A
ND
WA
STE
WA
TER
s pr
oduc
t m
ust
be a
dded
to
the
wat
er h
andl
ing
syst
em a
t a
poir
h as
the
area
of a
dditi
on o
f mak
e-up
wat
er to
the
hol
ding
tan
k.
1 — in
8l§§ 2-°-|S
T> t Q.
,2 c int j= 8co > §CO o
cu 7, ~a
thod o
f applic
atio
n:
CO
NTI
NU
OU
S I
NJE
CTI
ON
: A
dd t
his
prod
uct
at 3
0 pp
m a
ctiv
per
1000
gal
lons
of
wat
er)
whe
n sy
stem
is
no
ticea
bly
fouk
cont
rol
is e
vide
nt,
add
this
pro
duct
at
15 p
pm a
ctiv
e (2
0 flu
;ga
llons
of w
ater
) to
mai
ntai
n co
ntro
l.
o .S-
>> C CD O >,T3 —"CD .9 £ •" .a ji; o S.Ei§
ition
s, i
t is
des
irabl
e to
dilu
te t
he p
rodu
ct w
ith a
n ap
prop
riate
sol
vent
im
med
iaus
e. T
he c
once
ntra
tion
in t
he s
olve
nt m
ust
not
fall
belo
w a
n ac
tive
conc
entra
3f 5
00 to
5,0
00 p
pm b
ased
on
the
volu
me
of w
ater
in t
he p
ipel
ine.
Inj
ectio
ns t
oi m
ust b
e w
eekl
y, o
r as
nee
ded
to m
aint
ain
cont
rol.
GA
S S
TOR
AG
E W
ELL
S A
ND
SY
STE
MS
jal
inje
ctio
n w
ells
mus
t be
tre
ated
with
a s
uffic
ient
qua
ntity
of
this
pr
oduc
e co
ncen
tratio
n of
65-
1000
ppm
(on
an
activ
e qu
ater
nary
bas
is)
whe
n di
lute
dte
r pr
esen
t in
the
for
mat
ion.
Inj
ectio
n sh
ould
tak
e pl
ace
befo
re g
as i
s in
jec
the
sum
mer
). In
ject
ion
mus
t be
repe
ated
yea
rly o
r as
nee
ded
to m
aint
ain
cont
PIP
ELI
NE
PIG
GIN
G A
ND
SC
RA
PIN
G O
PE
RA
TIO
NS
is pr
oduc
t to
a sl
ug o
f wat
er im
med
iate
ly f
ollo
win
g th
e sc
rape
r (id
eally
thi
s w
?5
can
be k
ept
to a
min
imum
and
con
tain
ed b
etw
een
the
scra
per
and
the
trai
0 <1J <jj C "^ 3 > c
SlD ii H ^ 0 CD ^J - J - W C O - " c- i— (— T3co .0 L_I <n _ Q_ :t *ii-
all!(/3 5 T\ Q)
^ fl) ro (0
o in "c >
1 E H fl) jy
o o •- i£ ! 2 oCD ° "£ £
£ JB 8 o
« °.s aM*8Q. O o o
sflfc^ 1 CD °-c° •<• <5 m
S**§1SE E * § 5
1M3 !-"^ESilssgsS- l !m to .<2 ro °S 5 £ E <E
ts la-s2 </> £o 2£ § " 2 31— = cu ca .CI g,£t5<Q
lipim T- ? Q. o
Cvi
°£« 2E CD
% =en 14-
oco fc
CD E
r us
e in
oi
l fie
ld
and/
or
petro
chem
ical
w
ater
su
bsur
face
in
sond
ary
and/
or t
ertia
ry o
il re
cove
ry s
yste
ms
to
redu
ce t
he
nict
eria
, ae
robi
c ba
cter
ia,
sulfa
te-r
educ
ing
bact
eria
.
O CD COLL. in J2
•0 =!
<? °
0 CD
.£ o
I "Q- £
CO CD
CO enTJ CDtt) r=
DO
SIN
G L
OC
ATI
ON
(si
te o
f use
): T
his
prpd
uct
is t
o be
app
lire
cove
ry s
yste
m w
here
it
will
be
unifo
rmly
mix
ed,
such
as
at t
tank
s an
d ot
her
mix
ing
devi
ce l
ocat
ions
.
-
pig)
. S
uffic
ient
pro
duct
is a
dded
to
prod
uce
an e
ffect
ive
conc
entra
tion
of 7
5 -
500
pon
an
activ
e qu
ater
nary
bas
is (
9.6
to
64 o
unce
s pe
r 10
0 ga
llons
of w
ater
) de
pend
ing
the
leng
th o
f the
pip
elin
e an
d th
e se
verit
y of
the
biof
oulin
g..- 2?— CD
>. c<n co
£ °_ CD£ -Q
DO
SIN
G C
ON
DIT
ION
S:
This
pro
duct
sho
uld
be a
pplie
d w
heje
opar
dy
of
bein
g af
fect
ed.
Bad
ly
foul
ed
syst
ems
mus
ttre
atm
ent
is'b
egun
.
<v
% 11-CD in hr CD
f~ "^ CJ f—
DR
ILLI
NG
, C
OM
PLE
TIO
N A
ND
WO
RK
OV
ER
FLU
IDS
SY
STE
MS
oduc
t is
to
be a
pplie
d to
the
se f
luid
sys
tem
s at
a p
oint
of u
nifo
rm m
ixin
g, s
uch
latin
g ho
ldin
g ta
nk a
nd o
ther
mix
ing
devi
ce lo
catio
ns.
trea
tmen
t: A
dd 6
5 -
1000
ppm
(on
an
activ
e qu
ater
nary
bas
is)
of t
his
proc
31.5
gal
lons
of t
his
prod
uct p
er 1
00 b
arre
ls)
to a
fres
hly
prep
ared
flu
id.
Leve
ls•e
con
trol
will
var
y de
pend
ing
on c
ondi
tions
at
the
site
and
the
sev
erity
of
linat
ion.
nanc
e do
sage
: A
dd 6
5 -
1000
ppm
(on
an
act
ive
quat
erna
ry b
asis
) of
t (2
.1
to 3
1.5
gal
lons
of
this
pro
duct
per
100
bar
rels
) to
the
flu
id.
Leve
lse
cont
rol
will
var
y de
pend
ing
on c
ondi
tions
at
the
site
and
the
sev
erity
of
linat
ion.
5 3 _ o - - c . ay . ^ to n j -~o , ca C -^ " c j JS
0
EQ
UIP
ME
NT
US
ED
: U
se th
e in
ject
ion
pum
p to
app
ly th
e pr
odi
»
i'T3CO
£
R ri— f~
% R
US
E L
IMIT
AT
ION
S:
Dep
ende
nt u
pon
pH,
tem
pera
ture
and
acco
rdin
g to
con
ditio
ns f
ound
at t
he s
ite a
s ne
eded
to m
aint
ain
«
DO
SA
GE
AP
PLI
CA
TIO
NS
:
U)
§E %
(/)"(/) 03
88- 8§ CD |o £ ome oor^ — coCO J) CO
^.a Sa.
S
LUG
ME
THO
DIn
itial
Dos
e: W
hen
the
syst
em i
s no
ticea
bly
foul
ed,
appi
ppm
act
ive
ingr
edie
nt)
of th
is p
rodu
ct p
er 1
000
gal
lons
of \
App
ly fo
r 3
to 8
hou
rs d
aily
unt
il co
ntro
l is
achi
eved
.S
ubse
quen
t D
ose:
Whe
n m
icro
bial
con
trol
is e
vide
nt,
ad
E
>,
c
&
ppm
act
ive
ingr
edie
nt)
of th
is p
rodu
ct p
er 1
000
gal
lons
of
daily
or
as n
eede
d to
mai
ntai
n co
ntro
l.
r • (\ ~—T3 CO<D N(D '55
|*
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HI ill!!!Ill 111 {II 1 ! i illf1— o "o 5 1— ^ Q ^ o c . c L L l E Q . < u ^ a Q . o ) " r a < < - o c^c\ ico ^rio CD S < C o C Q < o . h - **~ > § T - r o ~ D
PA
CK
ER
FLU
IDS
This
pro
duct
is
to b
e a
dded
to t
he p
acke
r flu
id a
t a p
oint
of
unifo
rm m
ixin
g s
uch
as
aci
rcul
atin
g ho
ldin
g ta
nk a
nd
oth
er m
ixin
g de
vice
loc
atio
ns.
Add 2
.1 t
o 3
1.5
gallo
ns (
65 -
1000
ppm
act
ive
quat
erna
ry b
asis
) of
thi
s pr
oduc
t pe
r 10
0 ba
rrel
s of
pac
ker
fluid
. T
his
prod
uct
is ap
plie
d to
a
fres
hly
prep
ared
fluid
. Lev
els
for
effe
ctiv
e co
ntro
l w
ill v
ary
depe
ndin
g o
n co
nditi
ons
at t
he
site
and
the
sev
erity
of
the
cont
amin
atio
n.
Sea
l th
etr
eate
d pa
cker
flui
d in
the
wal
l be
twee
n th
e ca
sing
and
the
pro
duct
ion
tube
.
HY
DR
OT
ES
TIN
GT
reat
wat
er i
n t
he
hydr
otes
t pi
pelin
es or
ves
sels
with
65 -
1000
pp
m
on an
act
ive
quat
erna
ry
basi
s (0
.65
to
10
ga
llons
pe
r 1000
ga
llons
of
w
ater
) of
th
is
prod
uct,
depe
ndin
g on
the
wat
er q
ualit
y an
d le
ngth
of t
ime
the
equi
pmen
t will
rem
ain
idle
.
AU
XIL
LAR
Y S
ER
VIC
E W
AT
ER
AN
D W
AS
TE
WA
TE
R S
YS
TE
MT
his
prod
uct
is e
ffect
ive
for
the
cont
rol
of o
dor-
.form
ing
and
slim
e-fo
rmin
g ba
cter
ial,
fung
ian
d al
gae
in a
uxili
ary
serv
ice
wat
er s
yste
ms
such
as
fire
prot
ectio
n sy
stem
s an
d pu
mp
or s
cree
n ba
ys,
wat
er w
aste
sys
tem
s su
ch a
s st
orag
e ta
nks,
sto
rage
pile
s, a
ssoc
iate
dpi
ping
, se
tting
pon
ds o
r la
goon
s, t
rans
port
spi
llway
s or
can
als
and
disp
osed
wel
ls.
Add
5 -
180 p
pm
(ac
tive)
of
this
pro
duct
(4.
7 -
170.
3 ga
llons
per
3,00
0 ba
rrel
s of w
ater
)co
ntin
uous
ly.
Thi
s pr
oduc
t m
ust
be a
dded
to
the
sys
tem
at
a p
oint
of
unifo
rm m
ixin
g b
ysl
ug o
r in
term
itten
t fe
ed o
r by
spr
ayin
g on
to a
was
te p
ile.
The
fre
quen
cy o
f fee
d or
spr
ayan
d th
e du
ratio
n of
tre
atm
ent
will
de
pend
up
on
the
seve
rity
of t
he c
onta
min
atio
n.A
dditi
ons
to w
ater
sys
tem
s m
ust
be m
ade
durin
g t
he p
umpi
ng o
pera
tion
and
as
clos
e to
the
pum
p as
pos
sibl
e to
ens
ure
adeq
uate
mix
ing. ^^U -"C_5 ~
Q^ 'c* '
:Q| jZ *"* "-
||
'. ./ •!
SLI
MIC
IDE
AP
PLI
CA
TIO
NS
Thi
s pr
oduc
t ca
n be
use
d as
a s
limic
ide
in t
he m
anuf
actu
re o
f pa
per
and
pape
rboa
rd,
depe
ndin
g on
the
typ
e of
sto
ck,
qual
ity o
f ra
y w
ater
, co
mpl
exity
of
the
syst
em,
and
degr
ee o
f co
ntam
inat
ion.
App
ly t
his
prod
uct
inte
rmitt
ently
or
cont
inuo
usly
dep
endi
ng o
nm
ill c
ondi
tions
to
the
pap
er m
akin
g s
yste
m a
t a p
oint
of
unifo
rm m
ixin
g s
uch
as a
the
beat
ers,
thi
n or
thi
ck s
tock
che
sts,
br
oke
ches
t pu
mp,
sa
ve-a
ll ta
nk,
proc
ess
tank
or
Whi
tew
ater
tank
. D
o no
t us
e to
tre
at p
aper
or
pape
rboa
rd w
hich
will
con
tact
food
.
Initi
al
Dos
e:
Whe
n sy
stem
is
not
icea
bly
cont
amin
ated
, ad
d 4
to 8
00 p
ound
s of
thi
spr
oduc
t pe
r 10
0,00
0 ga
llons
of W
hite
wat
er to
be
trea
ted
(1.0
to
200
ppm
of
prod
uct)
as
aco
ntin
uous
or
slug
dos
e. R
epea
t un
til c
ontrol
is
achi
eved
. H
eavi
ly f
oule
d sy
stem
s m
ust
be b
oile
d ou
t pr
ior
to i
nitia
l tre
atm
ent.
Subse
quent
Dos
e:
Whe
n m
icro
bial
con
trol
is
evi
dent
, ad
d 1
to
100
gallo
ns o
f th
ispr
oduc
t pe
r 10
0,00
0 ga
llons
of
Whi
tew
ater
to
be t
reat
ed (
1.0
to 1
00 p
pm o
f pr
oduc
t) a
sne
cess
ary
to m
aint
ain
cont
rol.
CO
NT
RO
L O
F B
AC
TE
RIA
L, F
UN
GI/M
OLD
AN
D A
LGA
E O
N P
ULP
, P
AP
ER
BO
AR
D&
WE
T L
AP
Thi
s pr
oduc
t is
us
ed
to
inhi
bit
fung
al
grow
th,
whi
ch
caus
es
disc
olor
atio
n,
odor
and
degr
adat
ion
of
pape
r, pa
perb
oard
or
wet
lap.
App
licat
ion
of
this
pro
duct
mus
t be
mad
eat
a p
oint
in
the
syst
em w
here
mix
ing
actio
n is
goo
d. A
pplic
atio
n ca
n al
so b
e m
ade
atth
e si
ze p
ress
or
wat
er b
ox.
App
ly a
t a
rate
of
2 to
400
pou
nds
of th
is p
rodu
ct p
er t
on(d
ry b
asis
) of
pul
p or
pap
erbo
ard
prod
uced
.
Dosi
ng A
pplic
atio
n:
Thi
s pr
oduc
t m
ay b
e dr
ip f
ed c
ontin
uous
ly f
rom
the
dru
m,
dilu
ted
and
show
ered
to
the
wet
she
et o
r fe
d by
sui
tabl
e pu
mps
.
c
ill' ' '
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