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www.dezurik.com
BHP
RCV
ECC
VPB
RCV
ECC
VPB
KGV
KGV
KGV
KGV
KGV
KGV
KGV
KGV
KGV
VPB
VPB
VPB
VPB
BHPVPB BHP
VPB
VPB
PTW
VPB
VPB
VPB
VPB
VPBVPB
VPB
VPB
RCV
ECC
VPB
RCV
ECC
VPB
RCV
ECC
VPB
VPB
SAVEALL
SEAL CHEST
VPB
PTWPTW
PTWPTW
KGV
KGV
KGV
KGV KGV
KGV KGV
KGV KGV KGV KGV
PTW
BLENDCHEST
BROKECHEST
MACHINE
CHEST
SAVEALL
RECOVERED
STOCK CHEST
To Stuff Box
TICKLER REFINERS
REFINERS
Fro
m C
ou
ch P
it
From High
Density Storage
DilutionWater
LOWDENSITYSTORAGE
Fro
m P
ress
Pit
Fro
m P
ulp
er
SAVEALL
SAVEALL
FEED CHEST
DEFLAKERS
Dilution Water
Dilution Water
Paperstock
Dilution Water
ImpellerImpeller
Impeller
Impeller
SWEETENER
VALVE GUIDE FOR THE PULP & PAPER INDUSTRY
BULLETIN 97.01-01
MAY 2016
www.dezurik.com2 © 2016 DeZURIK, Inc.
The DeZURIK DifferenceThroughout our 250 years of combined history, DeZURIK, APCO, and HILTON have been recognized worldwide for collaborating with customers to design and engineer valves that provide superior performance and value. Each company was founded by an innovator who set out to solve a customer’s problem application.
DeZURIK’s founder, Matt DeZURIK, started designing products for the Sartell Paper Mill in 1925 that included knot boring machines, consistency transmitters and shower pipes. When he noticed that valves weren’t able to seal due to pitch build-up, he invented the first Eccentric Plug Valve – a design still in use today, dutifully solving sealing problems worldwide.
Today, the DeZURIK, APCO, and HILTON brands continue the tradition of partnering with our customers in the Pulp & Paper industry to provide the newest innovations in control, gate, plug, butterfly, automatic air and check valves. Our vision is to deliver exceptional value to our customers by applying our valve and problem-solving expertise to improve their operational performance.
Full-Featured Valves for Today ApplicationsDeZURIK recognizes the importance that control valves can play in process control performance and productivity. That’s why DeZURIK is dedicated to control valve testing. Regulating critical aspects of control valve performance such as accuracy, hysteresis, deadband and response time ensures that DeZURIK control valves provide optimum performance and help reduce costs.
Ruggedly Designed for Maximum ValueDeZURIK engineers spend many hours in the field listening to customers so they fully understand the intricacies of each application and incorporate that knowledge into each valve design. Using the latest advancements in technology such as Solid Modeling, Finite Element Analysis, 3D Rapid Prototyping and Computational Fluid Dynamics, DeZURIK engineers create valves that offer superior installed performance.
Quality Centered Manufacturing DeZURIK’s dedication to quality is demonstrated in all aspects of the business but foremost in our manufacturing capabilities. Our state-of-the-art CNC machining centers and large valve fabrication facilities allow us to produce in excess of 100,000 valves annually that range in size from 1/2" to 144" and weigh up to 40 tons. DeZURIK’s dedication to outstanding practices is ingrained in its culture, and exemplified in our quality system. DeZURIK has been certified to the ISO 9001 standard since 1996.
DeZURIK’s original Eccentric Plug Valve, developed in 1925 for the Sartell Paper Mill to solve a problem with pitch build-up.
DeZURIK High Performance Butterfly Valves are ideally suited for a wide variety of services including water, steam, liquor and other corrosive liquids and gases.
DeZURIK Knife Gate Valves and V-Port Ball Valves are widely used in pulping and stock prep operations throughout the mill.
www.dezurik.com 3
2-Year Manufacturer’s Warranty To further demonstrate our confidence in our product quality, DeZURIK offers a 2-Year Manufacturer’s Warranty as standard - double the length of time offered by most other manufacturers.
Wide Selection of Valve Styles DeZURIK has a wide variety of valve styles to meet the application requirements of the pulp and paper industry. DeZURIK manufactures valves for basis weight control, paper stock, liquor, steam, dilution water control and others. Valve styles that can handle everything from abrasive Kaolin clay slurries to recycle trash. The application guide charts on the following pages serve as a starting point in the valve selection process. For additional information or to contact your local representative, visit us at www.dezurik.com
Application Expertise You Can TrustThe application expertise of DeZURIK technical sales representatives, located throughout the world, will ensure you receive the personalized and complete service you need to keep your process performing at optimum levels. Our independent representatives are backed by over 500 DeZURIK employees at our factories, service centers and offices whose primary goal is customer satisfaction and maintaining long-term relationships.
DeZURIK’s Precision Electric Basis Weight Control Valve is specifically designed for critical paper stock control, and is used for basis weight and head box level control applications.
DeZURIK’s 3-Way Tapered Plug Valves are designed for throttling and diverting applications in refiner stock control applications.
DeZURIK’s versatile VPB V-Port Ball Valves are designed for highly accurate control of paper stock, in addition to other clean, dirty or corrosive liquids and gases.
Local Service and SupportDeZURIK Service Centers and local representatives maintain local inventory for quick delivery. Service Center and field service capabilities include automation, repair, reconditioning, emergency service, on-site scheduled maintenance and accuracy testing.
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4
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5
Leg
end
KG
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ate
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ve-
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s
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all V
alve
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ves
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er C
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ty K
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ve-
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ntr
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ater
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ater
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ry C
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am C
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er C
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ntr
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and
wh
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er
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6
RC
V
RC
V
RC
V
RC
V
Ro
tary
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ntr
ol V
alve
Co
ntr
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Bat
ch D
iges
ters
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t H
eati
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w B
ack
Val
ve
Wo
od
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ips
Liq
uo
rFe
edLi
neC
app
ing
Val
ve
150
psi
Ste
am
Liq
uo
rH
eate
rV
alve
Gas
Off
Val
ve
To
Blo
w T
ank
Blo
w V
alve
Dig
este
rs a
re u
sed
to
bre
ak d
ow
n t
he
wo
od
ch
ips
and
so
ften
th
eir
com
po
siti
on
. To
acc
om
plis
h t
his
, st
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o c
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lon
g w
ith
th
e ch
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wh
ite
and
bla
ck li
qu
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. Th
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mp
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incr
ease
d u
nti
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st
art
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do
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this
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th
e b
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val
ve is
o
pen
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nd
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ips
are
blo
wn
into
a t
ank
wh
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they
imp
act
the
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l an
d b
reak
into
fib
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dw
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TC
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ER
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7
Wo
od
Ch
ips
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ry C
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ve
Co
ntr
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ve
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r V
alve
150
psi
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am
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ack
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ve
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AT
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s an
d s
oft
en t
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mp
osi
tio
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om
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his
, st
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h t
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chip
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hit
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crea
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wh
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st
art
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reak
do
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. A
t th
is p
oin
t, t
he
blo
w v
alve
is o
pen
ed a
nd
th
e ch
ips
are
blo
wn
into
a t
ank
wh
ere
they
imp
act
the
wal
l an
d b
reak
into
fib
ers.
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ub
le-
Sea
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lV
alve
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pin
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alve
Han
dw
hee
l On
/Off
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8
KG
C-M
D
KG
C-M
D
KG
C-M
D
Max
imu
m D
uty
Kn
ife
Gat
e V
alve
To
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fuse
rP
ulp
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ck
To
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ove
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lack
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uo
r
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am
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am
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am
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ips
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mp
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ilter
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amin
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esse
l
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ircu
lati
on
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IRC
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ITH
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ND
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TE
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For
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yr d
iges
ter
valv
e ap
plic
atio
ns
con
tact
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UR
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licat
ion
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gin
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ite
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uo
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ash
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r
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ES
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R
TO
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AR
AT
OR
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yr C
on
tin
uo
us
Dig
este
r
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9
Rel
ief
Vap
or
SE
PA
RA
TO
R
Bla
ckLi
qu
or
Tu
rpen
tin
e
DE
CA
NT
ER
DIG
ES
TE
R
To
Sew
er
Wat
er
War
m W
ater
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ld W
ater
SE
PA
RA
TO
R
CO
ND
EN
SE
R
Sig
ht
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ss
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nd
ensa
te
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ck L
iqu
or
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erO
verf
low
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rpen
tin
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o C
ars
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rpen
tin
e
Tu
rpen
tin
e
Wat
er
Wat
er
Tu
rpen
tin
e R
eco
very
Sys
tem
VP
B
VP
B
VP
BV
-Po
rt B
all V
alve
VP
B
BH
P
VP
B
BH
P
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
Ecc
entr
ic P
lug
Val
veE
CC
EC
C
VP
BB
HP
EC
C
Co
ntr
ol
ST
OR
AG
E T
AN
KH
and
wh
eel O
n/O
ff
RC
V
RC
VR
ota
ry C
on
tro
l Val
ve
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10
Ch
ips
Ch
ip P
rest
eam
ing
Fres
hS
team
Steam And First Stage Pulp
Pro
cess
Ste
am Plu
g W
iper
Wat
erFr
esh
S
team
Dilu
tio
nW
ater
Tri
mD
iluti
on
Val
ve
Co
nsi
sten
cyT
ran
smit
ter
RE
FIN
ER
RE
FIN
ER
Ste
am R
eco
very
Sys
tem
Exh
aust
Feed
Th
erm
om
ech
anic
al P
ulp
ing
Pro
cess
(T
MP
)
KG
V
KG
V
RC
V
RC
V
RC
V
RC
V
EC
CV
PB
BH
P
VP
B
VP
BR
CV
VP
B
RC
V
EC
C
VP
B
VP
B
VP
B
VP
B
VP
B
RC
V
VP
B
CY
CLO
NE
KG
VK
nif
e G
ate
Val
ve
VP
BV
-Po
rt B
all V
alve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
Ecc
entr
ic P
lug
Val
veE
CC
RC
VR
ota
ry C
on
tro
l Val
ve
Co
ntr
ol
In t
his
met
ho
d o
f p
ulp
ing
, lo
gs
are
mec
han
ical
ly
chip
ped
an
d a
re s
oft
ened
wit
h s
team
. Th
e ch
ips
are
then
bro
ken
do
wn
into
fib
ers
in a
ref
iner
.
- Fr
esh
ste
am is
typ
ical
y 15
-30
psi
g, 2
50-2
80º
F-
Pro
cess
ste
am is
typ
ical
ly 6
0-75
psi
g, 3
00º
F-
So
me
fib
ers
are
pre
sen
t in
pro
cess
ste
am
KG
V
RE
FIN
ED
ST
OC
KC
HE
ST
Han
dw
hee
l On
/Off
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11
CY
CLO
NE
Ch
ips
Ch
ip P
re-
stea
min
g
Ch
emic
als
Reb
oile
rS
cru
bb
er
Pro
cess
Ste
am
Ste
am
Tri
mD
iluti
on
Val
ve
Ch
est
Dilu
tio
nV
alve
To
Mac
hin
e
Pu
lp
Pu
lp
Dilu
tio
nV
alve
Dilu
tio
nV
alve
1st
ST
AG
E R
EFI
NE
R
2nd
ST
AG
ER
EFI
NE
R
Feed
Ste
am
Cle
an S
team
to
Pap
er M
ach
ines
Ch
emic
al - T
her
mo
mec
han
ical
Pu
lpin
g (C
TM
P)
ST
OC
KC
HE
ST
Firs
t th
e w
oo
d is
mec
han
ical
ly c
hip
ped
. Th
e ch
ips
are
then
hea
ted
an
d c
hem
ical
ly t
reat
ed t
o
red
uce
th
e b
on
din
g p
rop
erti
es o
f th
e fi
ber
’s
lign
in a
nd
to
so
ften
th
em.
Tw
o c
hem
ical
p
roce
sses
are
use
d:
the
kraf
t p
roce
ss (
alka
line)
an
d s
ulf
ite
pro
cess
(ac
idic
).
KG
V
VP
B
VP
B
EC
C
KLS
RC
V
KG
VK
nif
e G
ate
Val
ve
VP
BV
-Po
rt B
all V
alve
Ecc
entr
ic P
lug
Val
veE
CC
KLS
Leve
l Sen
sor
Iso
lati
on
Val
ve
RC
VR
ota
ry C
on
tro
l Val
ve
VP
B
EC
C
EC
C
RC
V
VP
B
RC
VV
PB
VP
B
RC
VV
PBEC
CR
CV
VP
B
RC
VV
PB R
CV
VP
B RC
V
VP
B
RC
V
VP
B
RC
V
VP
B
RC
V
VP
B
VP
B
Leve
r O
n/O
ff
Han
dw
hee
l On
/Off
KG
V
Co
ntr
ol
Co
nsi
sten
cyT
ran
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ter
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12
To
Blo
w L
ines
Bla
ck D
iluti
on
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uo
r
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w H
eat
Rec
ove
ry
TrimDilutionValve
Bas
eD
iluti
on
Val
ve
Tri
mD
iluti
on
Val
ve
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wLi
ne
Fro
m
Dig
este
rs
Brown Stock
Bro
wn
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ck W
ash
ers
Dek
no
tter
Ho
t W
ash
Wat
er
SE
AL
BO
XE
SS
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LB
OX
ES
SE
AL
BO
XE
S
Th
ick
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ck P
um
p
To
Ble
ach
Pla
nt
or
Scr
een
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om
HIG
H-
DE
NS
ITY
ST
OR
AG
E
BLOW TANK
BLA
CK
LIQ
UO
RFI
LTR
AT
EV
ALV
ES
Wat
er
Aft
er t
he
sto
ck is
inje
cted
at
hig
h v
elo
city
into
th
e b
low
tan
k an
d t
he
chip
s ar
e b
roke
n d
ow
n
into
fib
ers,
a d
ekn
ott
er s
epar
ates
th
e ch
ips
and
kn
ots
. T
he
kno
ts a
re t
hen
dis
card
ed o
r se
nt
bac
k to
th
e d
iges
ters
fo
r fu
rth
er p
roce
ssin
g.
Th
e p
ulp
(co
oke
d f
iber
s) is
was
hed
to
rem
ove
re
sid
ual
liq
uo
rs t
hat
will
co
nta
min
ate
the
pro
cess
an
d a
lso
to
rec
ove
r th
e m
axim
um
am
ou
nt
of
chem
ical
s. T
he
spen
t ch
emic
als
that
are
rec
ove
red
go
to
sea
l bo
xes
and
th
en a
re
recl
aim
ed f
or
late
r u
se.
Th
e w
ash
ed p
ulp
is p
um
ped
into
hig
h-d
ensi
ty s
tora
ge
tan
ksan
d f
rom
th
ere
it g
oes
to
th
e b
leac
h p
lan
t o
r to
th
e sc
reen
ro
om
.
Imp
elle
r
BH
PV
PB
BH
P
VP
B
BH
P
VP
B
BH
P
VP
B
VP
B
Bro
wn
Sto
ck W
ash
ing
KG
V
KG
V
KG
V
KG
V
KG
O
Ecc
entr
ic P
lug
Val
veE
CC
KG
OO
-Po
rt G
ate
Val
ve
RC
VR
ota
ry C
on
tro
l Val
ve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
RC
V
VP
B
EC
C
RC
V
VP
B
EC
CR
CV
VP
B
EC
CR
CV
VP
B
VP
B
KG
VK
nif
e G
ate
Val
ve
VP
BV
-Po
rt B
all V
alve
Han
dw
hee
l On
/Off
Co
ntr
ol
Cyl
ind
er O
n/O
ff
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
13
RE
CO
VE
RY
BO
ILE
R
To
Sta
ck
Hig
h-D
ensi
tyB
lack
Liq
uo
rFr
om
Eva
po
rato
rs
CA
SC
AD
EE
VA
PO
RA
TO
RS
Bla
ck L
iqu
or
To
Rec
ove
ryB
oile
r
HE
AT
ER
S
Ste
am
Low
Pre
ssu
reS
team
Glo
be
Val
ve
Glo
be
Val
ve
Glo
be
Val
veB
lack
Liq
uo
r
Glo
be
Val
ve
Glo
be
Val
ve
Ste
am
Feed
Wat
er
Wea
k W
ash
Gre
en L
iqu
or
SM
ELT
DIS
SO
LVIN
GT
AN
K
Gre
enLi
qu
or
For
reco
very
bo
iler
app
licat
ion
s, c
on
tact
D
eZU
RIK
. Ap
plic
atio
n
En
gin
eeri
ng
.
Han
dw
hee
l On
/Off
Rec
ove
ry B
oiler
RC
VV
PB
VP
BV
-Po
rt B
all V
alve
Ecc
entr
ic P
lug
Val
veE
CC
RC
VR
ota
ry C
on
tro
l Val
ve
Co
ntr
ol
Cyl
ind
er O
n/O
ff
Th
e h
igh
ly c
on
cen
trat
ed b
lack
liq
uo
r is
sp
raye
d
into
th
e re
cove
ry b
oile
r an
d t
he
hea
t g
ener
ated
fr
om
th
is is
use
d f
or
mak
ing
ste
am t
o r
un
oth
er
par
ts o
f th
e m
ill. T
he
ino
rgan
ic s
mel
t th
at f
orm
s as
th
e b
lack
liq
uo
r is
bu
rned
flo
ws
to a
sm
elt
des
olv
ing
tan
k w
her
e it
is c
oo
led
an
d d
eso
lved
in w
ater
fo
rmin
g u
ncl
arif
ied
gre
en li
qu
or.
O-P
OR
T
O-P
OR
T O-P
OR
T
O-P
ort
Gat
e V
alve
ww
w.d
ezu
rik.
com
14
Rec
aust
isiz
ing
Are
a
To
Sew
er
Ho
t W
ater
or
Co
nd
ensa
te
Filt
rate
CA
US
TIS
IZE
RS
CLA
RIF
IER
Fro
m t
he
Sm
elt
Tan
k
Ste
am
Do
ub
le-
Sea
ted
Bal
lV
alve
HE
AT
ER
Full
Po
rtB
all V
alve
SLA
KE
R
Lim
e Fr
om
Kiln
LIM
EM
UD
TH
ICK
EN
ER
LIM
EM
UD
SLU
RR
Y
WH
ITE
LIQ
UO
RC
LAR
IFIE
R
ST
OR
AG
E
ST
OR
AG
E
CaC
O3
To
Dig
este
r
LIM
EM
UD
FILT
ER
To
Kiln
DR
EG
SW
AS
HE
R
GR
EE
NLI
QU
OR
Rec
aust
isiz
ing
is t
he
pro
cess
wh
ere
gre
en li
qu
or
(so
diu
m c
arb
on
ate
Na2
CO
3) is
co
nve
rted
into
w
hit
e liq
uo
r (s
od
ium
hyd
roxi
de
NaO
H).
Fir
st t
he
gre
en li
qu
or
is c
lari
fied
to
rem
ove
an
y d
reg
s,th
en t
he
lime
(CaO
) is
ad
ded
to
fo
rm w
hit
e liq
uo
r. N
ext,
th
e w
hit
e liq
uo
r is
cla
rifi
ed t
o r
emo
ve
lime
mu
d (
CaC
O3)
an
d is
ret
urn
ed t
o t
he
dig
este
rs f
or
coo
kin
g w
oo
d c
hip
s. F
inal
ly, t
he
rem
ove
d
lime
mu
d is
sen
t to
th
e lim
e ki
ln t
o f
orm
lim
e th
rou
gh
a h
igh
tem
per
atu
re r
eact
ion
.
RC
V
RC
V
RC
V
VP
B
RC
V
RC
VR
ota
ry C
on
tro
l Val
ve
Co
ntr
ol
Cyl
ind
er O
n/O
ff
VP
BV
-Po
rt B
all V
alve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
BH
P
Ecc
entr
ic P
lug
Val
veE
CC
EC
C
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
OR
TO
-PO
RT
O-P
OR
TO
-Po
rt G
ate
Val
ve
ww
w.d
ezu
rik.
com
15
Vap
ori
zers
To
Ble
ach
Pla
nt
Ble
ach
ing
- C
hlo
rin
e V
apo
riza
tio
n
VP
BV
-Po
rt B
all V
alve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
veR
CV
Ro
tary
Co
ntr
ol V
alve
Co
ntr
ol
RC
V
VP
B
BH
P
RC
VB
UFF
ER
TA
NK
Leve
r O
n/O
ff
RC
V
CO
MP
RE
SS
OR
CH
LOR
INE
TA
NK
CA
RC
HLO
RIN
ET
AN
K C
AR
Pad
din
g A
irC
hlo
rin
eB
all V
alve
s
Ch
lori
ne
Bal
l Val
ves
Air
FILT
ER
S A
ND
DR
YE
RS
Th
e b
leac
hin
g p
roce
ss u
ses
a va
riet
y o
f ch
emic
als
to
giv
e th
e p
ulp
its
des
ired
wh
iten
ess.
Ch
lori
ne
is o
ne
of
the
chem
ical
s u
sed
an
d r
equ
ires
sp
ecia
l han
dlin
g.
Mo
istu
re-f
ree
air
is u
sed
to
fill
tan
k ca
rs a
nd
tra
nsf
er
the
chlo
rin
e to
th
e b
leac
h p
lan
t.
Ste
am
ww
w.d
ezu
rik.
com
16
Ble
ach
Pla
nt
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
ort
Gat
e V
alve
RC
V
Ecc
entr
ic P
lug
Val
veE
CC
RC
VR
ota
ry C
on
tro
l Val
ve K
GV
Kn
ife
Gat
e V
alve
VP
BV
-Po
rt B
all V
alve
Co
ntr
ol
RC
V
RC
V
EC
C
VP
B
RC
VE
CC
VP
B
RC
V
EC
C
VP
BE
CC
VP
B
VP
B
VP
BV
PB
RC
V
RC
V
EC
C
VP
B
VP
B
VP
B
VP
B
RC
V
VP
BV
PB
VP
B
VP
B
Th
e b
leac
hin
g p
roce
ss o
ccu
rs in
mu
ltip
le s
tag
es. P
ulp
sto
ck c
an b
e w
hit
ened
by
eith
er
bri
gh
ten
ing
or
by
rem
ova
l of
the
lign
in a
nd
is a
cco
mp
lish
ed w
ith
th
e ad
dit
ion
of
chem
ical
s.T
he
pu
lp s
tock
is w
ash
ed b
etw
een
eac
h s
tag
e an
d s
tore
d. T
ypic
al b
leac
hin
g s
tag
es in
clu
de
chlo
rin
atio
n, a
lkal
ine
extr
acti
on
, oxy
gen
, hyp
och
lori
te, c
hlo
rin
e d
ioxi
de,
per
oxi
de
and
ozo
ne.
Stock Storage
STAGE 1 - Chlorination
STAGE 4 Chlorine Dioxide
STAGE 2
STAGE 3Hypochlorite
Ho
t W
ater
Fres
h W
ater
Ste
am
Was
her
Was
her
Was
her
Was
her
Tri
mD
iluti
on
Do
ub
le-S
eate
dB
all V
alve
Chlorine
Bas
eD
iluti
on
Bas
e D
iluti
on
HIGH-DENSITY TOWER
Tri
mD
iluti
on
Ble
ach
edS
tock
Sto
rag
e To
Pap
erM
ill
Cyl
ind
er O
n/O
ff
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
17
Sto
ck P
rep
arat
ion
an
d B
len
din
g O
verv
iew
BH
P
RC
V
EC
C
VP
B
RC
V
EC
C
VP
B
KG
V
KG
V
KG
V
KG
V
KG
V
KG
V
KG
V
KG
V
KG
V
VP
B
VP
B
VP
B
VP
B
BH
PV
PB
BH
P
VP
B
VP
B
PT
W
VP
B
VP
B
VP
B
VP
B
VP
BV
PB
VP
B
VP
B
RC
V
EC
C
VP
B
RC
V
EC
C
VP
B
RC
V
EC
C
VP
B
VP
B
SA
VE
ALL
SE
AL
CH
ES
T
VP
B
Co
ntr
ol
Cyl
ind
er O
n/O
ff
Han
dw
hee
l On
/Off
PT
WP
TW
PT
WP
TW
KG
V
KG
V
KG
V K
GV
KG
V
KG
V K
GV
KG
V K
GV
KG
V
KG
V
KG
VK
nif
e G
ate
Val
ve
VP
BV
-Po
rt B
all V
alve
3-W
ay P
lug
Val
veP
TW
PT
W
RC
VR
ota
ry C
on
tro
l Val
ve
Ecc
entr
ic P
lug
Val
veE
CC
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
3-W
ay H
and
wh
eel O
n/O
ffBLE
ND
CH
ES
TB
RO
KE
CH
ES
TM
AC
HIN
EC
HE
ST
SA
VE
ALL
RE
CO
VE
RE
DS
TO
CK
CH
ES
T
To
Stu
ff B
ox
TIC
KLE
R R
EFI
NE
RS
RE
FIN
ER
S
From Couch Pit
Fro
m H
igh
D
ensi
ty
Sto
rag
e
Dilu
tio
nW
ater
LOW
DE
NS
ITY
ST
OR
AG
E
From Press Pit
From PulperS
AV
EA
LL
SA
VE
ALL
FEE
D C
HE
ST
DE
FLA
KE
RS
Dilu
tio
n W
ater
Dilu
tio
n W
ater
Pap
erst
ock D
iluti
on
Wat
er
Imp
elle
rIm
pel
ler
Imp
elle
rIm
pel
ler
SW
EE
TE
NE
R
Co
nsi
sten
cyT
ran
smit
terC
on
sist
ency
Tra
nsm
itte
r Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
18
Cle
aner
s
Han
dw
hee
l On
/Off
Co
ntr
ol
VP
B
VP
B
VP
B
VP
B
VP
B
VP
B
VP
BV
-Po
rt B
all V
alve
PP
E
PP
E
Pre
cisi
on
Ele
ctri
c V
alve
Ecc
entr
ic P
lug
Val
veE
CC
EC
C
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
ve
Leve
r O
n/O
ffB
OS
Res
ilien
t S
eate
dB
utt
erfl
y V
alve
EC
C
EC
C
EC
C
EC
CE
CC
BO
S
BH
P
PA
PE
R M
AC
HIN
EW
HIT
E W
AT
ER
WE
LL
SE
AL
BO
XP
RIM
AR
YP
UM
P
VA
CU
UM
RE
CE
IVE
RT
AN
K
Op
tio
nal
Byp
ass
New
Sto
ckFr
om
Mac
hin
e C
hes
t
Bas
is W
eig
ht
Val
ve
Fro
m F
lat
Bo
x,S
eal B
ox
or
Sav
eall
PR
IMA
RY
CLE
AN
ER
S
Sample
Primary Supply
Flushing Line
Rej
ects
Hea
der
Pri
mar
y A
ccep
ts H
ead
er
Vac
uu
mR
elie
f V
alve
To
Sew
er
To
Sew
erSample
Sam
ple
Leve
l Co
ntr
ol V
alve
WH
ITE
WA
TE
R P
UM
P
TE
RT
IAR
YP
UM
P
TE
RT
IAR
YC
LEA
NE
R
SE
CO
ND
AR
YC
LEA
NE
RS
Byp
ass
Co
ntr
ol
Val
ve
Pri
mar
y, s
eco
nd
ary
and
ter
tiar
y st
age
clea
ner
s ar
e u
sed
in s
tock
p
rep
arat
ion
to
elim
inat
e al
l u
nw
ante
d m
ater
ials
.
SE
CO
ND
AR
YP
UM
P
Pri
mar
y A
ccep
ts T
o P
aper
Mac
hin
e H
ead
Bo
x
Acc
epts
Acc
epts
ww
w.d
ezu
rik.
com
19
Pap
er M
ach
ine
Wet
En
d
RC
VE
CC
BO
S
BH
P
KG
VK
LS
KG
VK
nif
e G
ate
Val
ve
VP
BV
-Po
rt B
all V
alve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
veP
PE
Pre
cisi
on
Ele
ctri
c V
alveP
PE
PP
E
RC
VR
ota
ry C
on
tro
l Val
ve
KG
V
VP
B
KG
V
BH
P
KG
V
VP
B
VP
B
RC
V
VP
B
VP
BV
PB
VP
B
VP
B
VP
B
BH
PV
PB
KLS
Leve
l Sen
sor
Iso
lati
on
Val
ve
Leve
r O
n/O
ff
Han
dw
hee
l On
/Off
Co
ntr
ol
Cyl
ind
er O
n/O
ff
BO
SR
esili
ent
Sea
ted
Bu
tter
fly
Val
veE
ccen
tric
Plu
g V
alve
EC
C
To
Sh
ow
ers
Sto
ck
MA
CH
INE
CH
ES
T
RE
FIN
ER
SC
RE
EN
S
Vac
uu
m
To
Bro
ke C
hes
t
Air
Pad
Lin
e
Wat
erS
EA
L B
OX
SE
AL
BO
X
Fan
Pu
mp
Bas
isW
eig
ht
Val
veHea
d B
ox
Leve
l Co
ntr
ol
Val
ve
Eff
luen
t
Wir
e
CLEANERS
HE
AD
BO
XT
o D
ry E
nd
MA
CH
INE
SIL
O
SA
VE
ALL
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
20
Fou
rdri
nie
r W
et E
nd
Alu
m
Glo
be
Val
ve
To
Sh
ow
ers
SA
VE
ALL
Wat
er
SE
AL
BO
XS
TU
FFB
OX
MA
GM
ET
ER
EFF
LUE
NT
WE
IR
Sew
erFr
om
Sto
ckP
rop
ort
ion
ing
Mix
ing
Ch
est
Dilu
tio
n W
ater
RE
FIN
ER
Bas
isW
eig
ht
Val
veFA
N P
UM
P
Ste
amS
EA
L B
OX
Wat
er
Bro
ke
To
Bro
keC
hes
t
To
Bro
ke C
hes
t
Dilu
tio
nW
ater
CLE
AN
ER
S
SC
RE
EN
S
Wire Pit
Wh
ite
Wat
erT
ank
MA
CH
INE
CH
ES
T
HE
AD
BO
XV
acu
um
Pu
mp
Ven
t T
o A
tmo
sph
ere
PU
LPE
R
Wir
eFl
at B
oxe
sP
ress
esT
o D
ryer
Co
uch
Ro
ll Co
uch
Pit
3-W
ay C
on
tro
l
BO
S
EC
C
VP
BV
-Po
rt B
all V
alve
Ecc
entr
ic P
lug
Val
veE
CC
3-W
ay P
lug
Val
veP
TW
RC
VR
ota
ry C
on
tro
l Val
ve
Co
ntr
ol
KG
V
VP
B
VP
B
VP
BP
TW
VP
BV
PB
VP
B
VP
B
RC
V
RC
V
EC
CV
PB
VP
BV
PB
VP
B
PP
EP
reci
sio
nE
lect
ric
Val
ve
PP
E
KG
VK
nif
e G
ate
Val
veB
HP
Hig
h P
erfo
rman
ceB
utt
erfl
y V
alve
BH
PB
OS
BH
P
BO
S
BH
P
BO
S
BH
P
BO
S
BH
P
Han
dw
hee
l On
/Off
KG
V
BO
SR
esili
ent
Sea
ted
Bu
tter
fly
Val
ve
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
21
RC
V
EC
C
Bas
is W
eig
ht
Co
ntr
ol
VP
B
KLS
VP
BP
PE
PP
E
PP
EP
reci
sio
nE
lect
ric
Val
ve
KLS
Leve
l Sen
sor
Iso
lati
on
Val
ve
RC
VR
ota
ry C
on
tro
l Val
ve
VP
BV
-Po
rt B
all V
alve
Ecc
entr
ic P
lug
Val
veE
CC
Leve
r O
n/O
ff
Co
ntr
ol
Hea
db
ox
Leve
l Val
veB
asis
Wei
gh
t V
alve
Dilu
tio
nC
on
tro
lV
alve
Leve
l Co
ntr
ol V
alve
MA
CH
INE
CH
ES
T
ST
UFF
BO
X
HE
AD
BO
X
Th
e b
asis
wei
gh
t va
lve
is u
sed
to
co
ntr
ol t
he
amo
un
t o
f st
ock
to
th
e h
ead
bo
x an
d is
po
siti
on
ed b
y th
e m
ill’s
Dis
trib
uti
ve C
on
tro
l Sys
tem
(D
CS
) o
r th
e g
aug
ing
sys
tem
wh
ich
mea
sure
s th
e d
ensi
ty a
nd
th
ickn
ess
of
the
fin
ish
ed s
hee
t o
f p
aper
.
Bas
is w
eig
ht
con
tro
l req
uir
es c
on
stan
t p
ress
ure
an
d c
on
sist
ency
to
th
e va
lve.
Alt
ern
ativ
ely,
th
is lo
op
may
be
con
tro
lled
by
a V
aria
ble
Fre
qu
ency
D
rive
(V
FD)
that
wo
uld
no
t re
qu
ire
a va
lve.
CO
MP
UT
ER
SY
ST
EM
CO
MP
UT
ER
SY
ST
EM
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
ww
w.d
ezu
rik.
com
22
Pap
er M
ach
ine
Dry
er S
ecti
on
CO
ND
EN
SA
TE
R
ET
UR
N S
YS
TE
M
VP
BV
-Po
rt B
all V
alve
BH
PH
igh
Per
form
ance
Bu
tter
fly
Val
veR
CV
Ro
tary
Co
ntr
ol V
alve
Co
ntr
ol
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
VB
HP
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
RC
V
BH
P
VP
B
Ste
am T
o D
ryer
s
Ste
am W
edg
e G
ates
Mak
e U
pW
ater
Fro
m W
et E
nd
SE
PA
RA
TO
RS
EP
AR
AT
OR
SE
PA
RA
TO
RS
EP
AR
AT
OR
SE
PA
RA
TO
R
Co
nd
ensa
te T
o M
ill
VA
CU
UM
RE
CE
IVE
R
VA
CU
UM
CO
ND
EN
SE
R
Th
e p
aper
mac
hin
e d
ryer
rem
ove
s an
y re
sid
ual
wat
er t
hro
ug
h e
vap
ora
tio
n a
s th
e sh
eet
pas
ses
thro
ug
h
hea
ted
ste
am r
olle
rs. A
co
nd
ensa
te s
yste
m c
olle
cts
wat
er f
rom
th
e st
eam
fo
r re
use
in t
he
mill
. In
ord
er
to r
edu
ce e
ner
gy
con
sum
pti
on
, wat
er is
co
nti
nu
ally
reu
sed
in t
he
mill
. At
the
dry
en
d o
f th
e p
aper
m
ach
ine,
sep
arat
ors
pu
ll w
ater
into
th
e m
ill‘s
co
nd
ensa
te s
yste
m f
or
even
tual
reu
se.
Flas
hS
team
Ste
amW
edg
eG
ates
Ste
amW
edg
eG
ates
Cal
end
ar
ww
w.d
ezu
rik.
com
23
Sec
on
dar
y Fi
ber
Rep
ulp
ing
VP
BEC
C
RC
V K
GV
BH
P
V-P
ort
Ba
ll V
alve
Ecc
entr
ic P
lug
Va
lve
Ro
tary
Co
ntr
ol V
alv
eS
pli
t G
ate
Kn
ife
Gat
e V
alv
eH
igh
Pe
rfo
rma
nce
Bu
tter
fly
Va
lve
Co
ntr
ol
Han
dw
hee
l On
/Off
Cyl
ind
er O
n/O
ff
Leve
r O
n/O
ff
VP
B
VP
B
VP
BEC
C
ECC
VP
BEC
CR
CV
VP
B
ECC
RC
V
VP
B
ECC
RC
V
VP
BEC
CR
CV
KG
V
KG
V K
GV
KG
V
KG
V
KG
V
KG
V
KG
V
SG
O-P
ort
Gat
e V
alve
O-P
OR
T
SG
KG
V
SG
KG
V
SG
KG
V
SG
KG
V
BH
PV
PB
BH
PV
PB
ECC
BH
PV
PB
O-P
OR
T
O-P
OR
T
O-P
OR
T
O-P
OR
T
Wat
er H
ead
er
Rag
ger
Wh
itew
ater
He
ad
er
Tra
shB
ales
PU
LPE
R Imp
elle
r
Acc
epts
Pu
mp
Rej
ects
CLEANER
Pu
mp
Ba
se D
iluti
on
Bas
e D
iluti
on
Tri
m D
iluti
on
TH
ICK
EN
ER
ST
OC
KC
HE
ST
Dir
t T
rap
Dir
t T
rap
Tri
mD
iluti
on
Bal
lV
alve
Tra
sh
Tra
sh
Tra
sh
VIB
RA
TO
RS
CR
EE
NS
SC
RE
EN
PLA
TE
SU
RG
EC
HE
ST
Sec
on
dar
y fi
ber
is a
ny
fib
rou
s m
ater
ials
b
ein
g r
epu
lped
as
a ra
w m
ater
ial t
o
rem
anu
fact
ure
into
a n
ew p
rod
uct
.
KG
C-M
D
KG
C-M
D
Max
imu
m D
uty
Kn
ife
Gat
e V
alve
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
Co
nsi
sten
cyT
ran
smit
ter
DeZURIK, Inc. s the right to incorporate our latest design and material changes without notice or obligation. Design features, materials of construction and dimensional data, as described in this bulletin, are provided for your information only
and should not be relied upon unless confirmed in writing by DeZURIK, Inc. Certified drawings are available upon request.
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