Macro Stickies and Screening Background Research Objective Results and Discussion PSA Particle Screening PSA Particle Breakage PSA Particle Extrusion Overall Conclusions Future Research
Macro Stickies and Screening
Background
Research Objective
Results and Discussion
PSA Particle Screening
PSA Particle Breakage
PSA Particle Extrusion
Overall Conclusions
Future Research
Pressure Sensitive Adhesives
Pressure sensitive adhesive base polymers consist of acrylic or rubber-based polymers
Glass transition temperature is below room temperature and depends on the adhesive formulation
Young’s modulus and shear strength are low and depend on the adhesive formulation and the system temperature
Pressure Screening
Pressure screening is
considered to be the most
effective way to remove
adhesive contaminants from
pulp
Typical removal efficiencies
of adhesive contaminants
range from 50 to 80% for
commercial pressure screens
Analysis of Stickies -- SOWM. A. Pikulin, AF&PA and USPS Joint Conference to
Address PSA Issues, June 1996
0
5
10
15
20
25P
ulp
er
'Scre
en
"S
cre
en
Flo
tn.
Pro
du
ct
Styrene-Acrylate
SBR
PVAC,EVA
Acrylate
SIS Copolymer
Particle Breakage
Breakage of PSA particles depends on the:
Shear/tensile strength of the PSA
Shear/tensile forces in the device
If the forces in the device are greater than
the strength of the PSA material, then the
PSA material will break
Research on Screening of Stickies
Studies of the effects of operating parameters and
equipment on removal efficiency by: Consistency, slot velocity, and slot width [Vitori, Pulp and Paper
Canada, 1993]
Reject rate, rotor speed, and slot velocity [Heise, Tappi Journal,
1992]
Consistency, reject rate, rotor speed, slot velocity, and slot width
[Seifert, et. al., 5th Research Forum on Recycling, 1999]
Consistency, rotor speed, slot velocity, and slot width [Saint Amand
and Perrin, Tappi 1998 Pulping Conference, 1998]
Results from Previous Research
Removal efficiency increased to a maximum at an optimum consistency
Removal efficiency increased as the:
Reject rate increased
Rotor speed, slot velocity, or slot width decreased
Weaknesses in the studies were:
Undefined materials
Relationships between efficiency and operating conditions were defined but not explained
Little insight provided on the mechanism of passage
Outline
Background
Research Objective
Results and Discussion
PSA Particle Screening
PSA Particle Breakage
PSA Particle Extrusion
Overall Conclusions
Future Research
Research Objective
To understand how the operating
conditions and adhesive formulation
affect the passage of pressure sensitive
adhesive particles in industrial and
laboratory screens
Outline
Background
Research Objective
Results and Discussion
PSA Particle Screening
PSA Particle Breakage
PSA Particle Extrusion
Overall Conclusions
Future Research
PSA Particle Screening
Do pressure sensitive adhesive particles
behave differently in industrial pressure
screens than in laboratory screens?
Approach: Study the removal of pressure
sensitive adhesive particles by an industrial
pressure screen and laboratory screens
Pilot Plant Layout
Rejects
Flow
Meter
Pump
Industrial
Screen
Feed
Stock
Tank
Second
Stock
Tank
Accepts
Shower
Screening Parameters:
1% Consistency, 50oC,
0.006 in. wide slots,
Mass Reject Ratios of
4.5%, 12%, 15%, and 25%
Lab scale screening
Valley Flat Screen
0.006 in. slots
25oC, 45oC
Pulmac
MasterScreen
0.006 in. slots
25oC
Accepts
Accepts
Rejects
Rejects
Pilot Plant
Pulper
Samples
Detection of Stickies
Handsheet
Morplas Blue - Heptane Dye Solution
Dyed
Handsheet
for Image
Analysis
Cleanliness Efficiency of
Industrial and Laboratory Screens
0
20
40
60
80
100In
du
stri
al,
RR
=4
.5%
Ind
ust
rial,
RR
=1
2%
Ind
ust
rial,
RR
=1
5%
Ind
ust
rial,
RR
=2
5%
Pu
lmac,
25
C
Vall
ey
,
25
C
Vall
ey
,
45
C
Screening Devices
Cle
an
lin
ess
Eff
icie
ncy
, %
PSA Particle Screening
Do pressure sensitive adhesive particles behave differently in industrial pressure screens than in laboratory screens?
Yes, pressure sensitive adhesive particles behave differently in industrial pressure screens (40-70% efficiency) than in laboratory screens (99% efficiency).
Outline
Background
Research Objective
Results and Discussion
PSA Particle Screening
PSA Particle Breakage
PSA Particle Extrusion
Overall Conclusions
Future Research
PSA Particle Breakage
Do PSA particles breakdown in the industrial pressure screen?
Approach: Analyze the PSA particles before and after the industrial pressure screen
Intense Forces in a Industrial Slotted Pressure Screen
Break/Deform Adhesives: Decreases Screening Efficiency
Pressure
Screening
10
100
1,000
10,000
<0.50 0.50-
1.00
1.00-
1.50
1.50-
2.00
2.00-
2.50
2.50-
3.00
>3.00
Particle Size, mm2
Pa
rti
cle
s i
n 1
m2
Feed
Accepts +Rejects
“Thousands of small
particles generated”
Shredding
makes
particles more
1-dimensional
Screen Removal Efficiency
Versus Particle Size
-1500
-1300
-1100
-900
-700
-500
-300
-100
100
<0.50 0.50-
1.00
1.00-
1.50
1.50-
2.00
2.00-
2.50
2.50-
3.00
>3.00
Particle Size Ranges, mm2
Reje
ct
Eff
icie
ncy,
%
RR=4.5%
RR=10%
RR=15%
RR=25%
PSA Particle Breakage
Do PSA particles breakdown in the
industrial pressure screen?
Yes, PSA particles do breakdown in the
industrial pressure screen.
PSA Particle Breakage
Which operating parameters in an industrial
pressure screen have the most significant effect
on the breakage of PSA particles?
Approach: Conduct a statistical analysis
experiment using a high intensity laboratory mixer
simulating forces in a screen with PSA particles
Experimental Procedure
Pilot Plant Pulper
10% K, 45oC, 20 min
80 OD lbs.
Copy Paper with
Adhesive Labels
(1% by wt.)
Samples
Quantum
High Shear Mixer
3 Liters
(vary parameters)
Handsheets
Dyeing
Image Analysis
Operating Parameters
Full Factorial Design Experiment with a
Center Point
Variable Low Value Center Point High Value
Pulp Consistency,% 3 7.5 12
Mixing Time, seconds 30 165 300
Initial Temperature, oC 20 35 50
Rotor Speed, rpm 600 1500 2400
0
300
600
900
1200
1500
1800
2100
CO
NS
TIM
E
TE
MP
RO
TO
R
CO
NS
TIM
E
CO
NS
TE
MP
CO
NS
RO
TO
R
TIM
ET
EM
P
TIM
ER
OT
OR
TE
MP
RO
TO
R
CO
TIT
E
CO
TIR
O
CO
TE
RO
TIT
ER
O
CO
TIT
ER
O
Variable
|Eff
ect|
2 Limit
Pareto Analysis: Number of PSA Particles
Versus Operating Variables
Number of Particles in 1 m2
vs. Consistency
0
4000
8000
12000
16000
0 4 8 12 16
Consistency, %
Nu
mber
of
Par
ticl
es in
1 m
2
Treated
Untreated
Number of Particles in 1 m2
vs. Initial Temperature
0
2000
4000
6000
8000
10000
12000
0 20 40 60 80
Initial Temperature, oC
Nu
mber
of
Par
ticl
es in
1 m
2
Treated
Untreated
Average Particle Size
vs. Time
0.00
0.20
0.40
0.60
0.80
1.00
0 60 120 180 240 300 360 420
Time, seconds
Aver
age
Par
ticl
e S
ize,
mm
2
Treated
Untreated
PSA Particle Breakage
Which operating parameters in an industrial pressure screen have the most significant effect on the breakage of PSA particles?
The operating parameters of consistency, time, and temperature have the most significant effect on the breakage of PSA particles.
PSA Particle Extrusion
How do the pressure difference across the
slot and operating temperature affect
particle passage through a slot?
Approach: Measure the pressure difference
at which PSA particles pass through the slot
of a pressurized single slot device at
different temperatures
Experimental Procedure
450H Pulper
12% K, 45oC,
415 rpm, 60 min
450 OD g of paper
10 adhesive labels
Single Slot Device
0.18 mm wide slot
Single Slot Device Procedure
Remove a PSA particle from pulp
Measure the dimensions of the PSA particle under a microscope
Place the PSA particle on the slot
Add 1000 mL of deionized water
Slowly open the vacuum line valve to increase the pressure difference across the slot
If the particle passes through the slot, record the vacuum pressure at which the particle passes through the slot
Top View
Side View
PIV
a
c
u
u
m
Commonly Observed
Particle Passage Process
Increasing Pressure Difference
indicates
Cumulative Particle Passage
Versus Pressure Difference
0
20
40
60
80
100
0 20 40 60 80
Pressure Difference, kPa
Cu
mu
lati
ve
Par
ticl
e P
assa
ge,
%
5C
20C
50C
Typical Pressure Differences in an
Industrial Pressure Screen*
*Bliss, T., and Ostoja-Starzewski, M., 1997 Tappi Korea Recycling Symposium, pp. 1-17, 1997.
PSA Particle Extrusion
How do the pressure difference across the
slot and operating temperature affect particle
passage through a slot?
Increasing the pressure difference across
the slot or the operating temperature
increases particle passage through a slot.
PSA Particle Extrusion
Do the mechanical properties of the PSA formulations affect the passage of PSA particles through a slot?
Approach: Analyze particle passage in the
single slot device for PSA films with
different formulations
Experimental Procedure
450H Pulper
12% K, 45oC,
415 rpm, 30 min
450 OD g of paper
6 adhesive labels
Single Slot Device
0.18 mm wide slot
Particle Passage Versus Particle Area for
Eight Different Formulations
0
20
40
60
80
100
0.0 1.0 2.0 3.0 4.0
Calculated Particle Area, mm2
Cum
ulat
ive
Par
ticl
e P
assa
ge, % BA BA:A
BA:G BA-EA
BA-EA:A BA-EA:G
AC SIS
Calculated (Yield Stress and Area)
Versus Actual Particle Passage
0
20
40
60
80
100
0 20 40 60 80 100
Actual Particle Passage, %
Cal
cula
ted
Par
ticl
e P
assa
ge,
%
PSA Particle Extrusion
Do the mechanical properties of the PSA formulations affect the passage of PSA particles through a slot?
Answer: yes, yield strength and size are
the most critical properties
Overall Conclusions
PSA particles break down in industrial
pressure screens
Consistency, temp and time affect breakage
PSA particles extrude in industrial pressure
screens
Pressure drop, temp, and particle size and
stiffness affect passage