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Global Trends Effecting the Design of Retention Aid ProgramsLarry Hutchinson
Solenis LLC
IPPTA – “Enhancing Productivity, Quality, Value Addition, and Environmental Sustainability Through Specialty Chemicals”
Resort Rio, Goa, India, 19-20JUL2019
2 • Confidential and proprietary.
Global Trends
Importance of Retention
System Closure
Multifunctional Chemistry and the Crowded Wet End
3 • Confidential and proprietary.
Magic!
4 • Confidential and proprietary.
Water
Food Safety
EHS/
Hygiene
g/m²
Speed
Furnish
Complexity
Furnish
Strength
Ash Content
ContaminationVariation
Dewatering
pH
CaCO3
Temperature
Conductivity
Scale
System Charge
Functional Chemistry
Process Chemicals
5 • Confidential and proprietary.
34.0
35.0
36.0
37.0
38.0
39.0
Mill A Mill B Mill C Mill D Mill E Mill F Mill G Mill H Mill I Mill J
35# HPL - Basis Weight Comparison
Low BW for a totally
closed mill, but also the
slowest machine in this
survey @ 1900 fpm
Closed Open
Impact of Mill Closure on Sheet Strength
6 • Confidential and proprietary.
Retention Programs
Deposit Control
Drainage/Dewatering
Chemical Efficiency
What is the job of a paper machine?
7 • Confidential and proprietary.
Liquid/Solids Separation
Fiber Furnish & Contaminants
Filler
Water
Broke & Contaminants
Functional Additives:
DSA, Size, WSR, Dyes
Process Chemicals:
RDC, MB, AF/DF, CC
Accumulation = Efficiency Loss + Deposition
Sheet
Stock
PrepFormer Press
control of system inputs
and purge points
8 • Confidential and proprietary.
Softwood Fiber
Length = 3500 µm (50’)
So
ftw
oo
d F
iber
Wid
th=
36
µ m
PrecipitatedCalcium Carbonate
0.2-2.0 µm
Size
1 µm
Hardwood Fiber
Length = 1200 µm (17’)
Hard
wo
od
Fib
er
Wid
th =
22
µm
Pitch Particle
Dispersed
0.1 µm
Calcium Carbonate
Ground
0.2-5.0 µm
Titanium
Dioxide
0.1-1.0 µm
Small Fiber Fine
5 X 15 µm
Flocculant
0.1m µm
Coagulant
0.05 µm
Clay
0.3-2.0 µ m
“retention” is
not about just
one material
9 • Confidential and proprietary.
Size, Shape, Surface Chemistry
Kaolin Clay @ 8500x Talc @ 5000x Chalk @ 4500x TiO2 @ 10,000x
Rhombohedral PCC @4500x Aragonite PCC @ 4500x Scalenohedral PCC @ 4500x GCC @ 5000x
Increasing use of fillers
can place tremendous
demands on the
retention system. Filler
characteristics can vary
widely and should be
carefully factored into
the overall retention
system design.
10 • Confidential and proprietary.
100
50
75
25
0
INC
RE
AS
ING
RE
TE
NT
ION
INCREASING PARTICLE SIZE
Thickening & Filtration
Mechanism
Mechanical
AbsorptionMechanism
Chemical
CLAY, GCC
0.5-20 µm
WIRE SIZE150 MESH
FINES
<75 µm
TiO2, PCC
0.2 - 0.5 µm
LONG FIBER &
FIBER FRAGMENTS
Not only is retention
important but how
materials are retained,
how that effects where
they end up in the sheet
and impacts on drainage
and dewatering are
critical.
11 • Confidential and proprietary.
Sheet Forming
Water
Fiber
Fines
Filler
Stickies & Pitch
Sizing
Starch
Retention Aid
Water
Fines
Filler
Stickies
Other Stuff
12 • Confidential and proprietary.
The Retention Paradox
Cost
Deposits
Speed
Strength
… how low can we go?
13 • Confidential and proprietary.
Consequences of system closure …
HBMCBCTo
wer
Pre
ss
Polydisc
Short Loop
Long Loop
Cleaning
Th
ick
en
ing
Fib
er p
rod
.
Broke
Conductivity
Speed
Strength
Additives Efficiency
Additives Effectiveness
Deposition
14 • Confidential and proprietary.
14
Bull
Screen
Chest
GWD
ThickenersGrinders
RCF
Tower
GWD
WW
Chest
WW
Chest
Screening &
Cleaning
GWD
Thickener
Chest
PM GWD
TowerGWD
Storage
Tower
GWD
Storage
Tower
PM Broke
Tower
UBKP
NBKP
TL BC
FL BC
BL BC
TL MC
FL MC
BL MC
TL Former
FL Former
BL Former
TL WW FL WW BL WW
OCC, MXW
Dry Broke(contains clay,
CaCO₃, starch,
latex from coating)
Wood
Fresh Water
Fresh Water
Perform PK 2320
Alum
PK 2320
Na2S2O4
6kg/t
Coating Effluent
Caustic
PC8717
Refining
Refining
DF
Alum
NaHCO₃
H₂SO₄
Clay
Biocide
Biocide
Biocide
Biocide
Biocide
Aquapel AL215/
Hi-pHase 40T
Biocide
Na2S2O4
(NNIU)
Couch Pit
System Overview - Major Chemical and Furnish InputsNote: Does not include wet end defoamer which is used intermittently, or
thin stock RDC
Map the system
and understand the
dynamics
System Closureconductivity is a marker …
16 • Confidential and proprietary.
System Closure
• Use the cleanest water you can get▪ Surface vs. bore well▪ Clarification
• Strategic use of low conductivity water streams
• Minimize high conductivity input streams
• Purge the most highly contaminated water
• ”Kidneys”▪ Clarification▪ Membrane filtration
• Chemistry selection for high conductivity systems▪ Nothing gets better with conductivity▪ The problem may be more to do with lignin or other soluble materials than conductivity▪ Get outside the box on flocculant selection▪ Trash management/Lignin management
17 • Confidential and proprietary.
Industry Experience
Chemical Efficiency
T&T
Recycled Container
Virgin Container
Conductivity: ~1,000
Conductivity: 5,000+
Conductivity: ~2,500
Does conductivity
adequately explain
the loss in chemical
efficiency?
18 • Confidential and proprietary.
Organic vs. Inorganic Comparison
▪ Higher organic concentration negatively impacted drainage / chemical efficiency
▪ Higher conductivity (inorganics) had a minimal impact to drainage / chemical efficiency
Organic load had a much greater impact
on chemical efficiency compared to
inorganic load (conductivity)
19 • Confidential and proprietary.
Effect of Lignin on Polymer Efficiency
Increasing lignin reduces
impact of drainage aid
20 • Confidential and proprietary.
Typical papermaking … more than one factor!
Chemical Efficiency
T&T
Recycled Container
Virgin Container
Conductivity: 1,000
Lignin: <30ppm
Conductivity: 5,000+
Lignin: 50-600ppm
Conductivity: 2,000
Lignin: 100-2200
Loss in chemical
efficiency is better
explained by increasing
soluble lignin content.
21 • Confidential and proprietary.
Lignin Management in Unbleached Kraft
Key Finding: Improving polymer efficiency requires
lignin removal, not conductivity reduction
The Challenge:
▪ Packaging Growth and Sustainability Drivers are
Creating a Need for More Effective Chemical
Solutions
▪ Wet end chemistry struggles in most unbleached
Kraft furnishes
Key Learnings:
▪ Organic contaminants, namely lignin, have a much
greater effect on chemical efficiency than inorganic
▪ Lignin can be monitored, controlled and managed to
improve performance of wet end chemistry
▪ Some chemistries are more resilient to lignin than others
▪ Significant lignin removal from the soluble phase is
possible and can greatly increase chemical efficiency
▪ Program design can be improved with Lignin
Management approach
Additives Multifunctional Role and Impact on Retention Chemistry
Strength
DrainageRetention
Fusion
23 • Confidential and proprietary.
Multi-Functional Chemistry & Trends
• Coagulants/Fixatives
▪ Inorganic
• Alum, PAC
▪ Organic
• Polyamines, polyDADMAC, PEI
• Flocculants
▪ Cationic, anionic, non-ionic
• Aqueous Dispersed Polymers
• Enzymes
• Dry Strength Additives
▪ Starch, APAM, CPAM, AmPAM, PVAM, GPAM,
on-site GPAM
• Wet Strength Additives
• “Microparticles”
▪ Silica Based Microparticles
• Structured, Surface Modified, On-site generation
▪ Bentonite
▪ Structured Polymers
• Coated Broke Treatment
• Furnish Pre-Treatment
• Filler Pre-Treatment
• Sizing
▪ Rosin, AKD, ASA
• Surface Applications
▪ Sizing
▪ DSA’s
24 • Confidential and proprietary.
Retention Program Design Considerations
• Furnish components have wildly different capacities for “chemistry”
• RCF: content ➚, strength ➘, ash content & contamination ➚
• CaCO3 ➚, pH ➚
• Sheet ash ➚
• g/m² ➘, speed ➚
• … the wet end is a lot more crowded and challenging place!
25 • Confidential and proprietary.
Going neutral/alkaline changes the alum scenario …
Using alum at alkaline pH requires understanding what you want to do with it and getting the dose point(s)
right. PAC and or cationic polymers are often a better option.
26 • Confidential and proprietary.
Balancing System “Charge”
“Charge” (Soluble, Total, Colloidal)
“0”
“R
ete
nti
on
”
“-” “+”
“Threshold Charge”
behavior, just need to
keep charge above a
minimum or chemical
is wasted.
“Sweet Spot
Charge” behavior,
ideal charge range
for stable retention.
Retention theory says best retention
should be with charge near “0” but …
Sensitive to cationic
demand, narrow
operating window
Less sensitive to
cationic demand, wider
operating window
27 • Confidential and proprietary.
Dosing Regime, Injection, Mixing
Primary
Screen
Fan
Pump
Cationic Starch
or DSA
Flocculant
Structured Silica
VMAX
Injection
VMAX
Injection
VMAX
Injection
Dry Strength
Structured Polymer
Sizing
Alum or
PAC
Alum or
PAC
Wide variety of options, key
is choosing correct
scenario for planned
chemistry and insuring
good mixing with best
practice injection
technology.
Best practice injection
and mixing technology
enables a greater
number of dosing
options post-screen
which greatly increases
performance
Thick/thin dual DSA
addition.
Filler pre-treatment
Broke Pre-Treatment
Stock Pre-Treatment
Dilution water
quality matters;
• Hardness
• Conductivity
• Temperature
• pH
28 • Confidential and proprietary.
Think multi-component retention systems …
#2Polyacrylimide
Addition
(Bridging /
Flocculation)
Process
Generated
Shear
#3Structured Silica /
Structured Polymer
Addition
(Micro-flocculation)
#1Coagulation,
Cationic
Demand
Modification
+ +
+
++
+
++ + +
++
++
+
Thick/thin dual DSA
addition.
Filler pre-treatment
Broke Pre-Treatment
Stock Pre-Treatment
Multi-component, high
performance retention
systems integrated with
…
Filler pre-Treatment
30 • Confidential and proprietary.
Filler pre-treatment … balancing strength & loading
TreatedFiller
BondingPolymer
Fiber
1)
2)
Aggregation Polymer
Filler
31 • Confidential and proprietary.
Optimal Particle Size Distribution
0
1
2
3
4
5
6
7
1 10 100 1000
Freq
uenc
y %
Diameter µm
Particle Size with Treated PCC
Blank Filler-Fiber Optimization Over aggregation
• Moderate aggregation targeted for optimal strength, retention and optical properties• Aggregates are shear stable
0
2
4
6
8
10
12
14
16
18
20
0 5 10 15 20 25 30 35
Fre
qu
ency
%
Diameter µm
Particle Size with Treated PCC
Filler-Fiber Optimization plus 1 min sonication
32 • Confidential and proprietary.
Pilot machine results: Filler-Fiber optimization program can maintain ZDT
Tensile and ZDT Impact
15
17
19
21
23
25
27
15 17 19 21 23 25 27 29
GM
T N
∙m/g
Ash %
Dry Tensile on 50 lb/3000 ft² Paper
Blank Bonding Bonding &Aggregation
40
45
50
55
60
65
15 17 19 21 23 25 27 29
lb/i
n²
Ash %
ZDT on 50 lb/3000 ft² Paper
Blank Bonding Bonding &Aggregation
33 • Confidential and proprietary.
• Handsheet data showing wet web tensile (on never dried sheets)
• Loss recovered with aggregation + bonding approach
Wet Web Strength
0
0.2
0.4
0.6
0.8
1
Ten
sile
lbf
Tensile on Never Dried SheetsSheet Solids 50%; PCC 20 30%
Untreated 20% Untreated 30% 30% Filler-Fiber Optimization Program
34 • Confidential and proprietary.
Z-directional Filler DistributionImproved Distribution with Higher Filler Content
• Uniform z-directional filler distribution helps limit dusting tendency.• More potential for filler increase.
20
25
30
35
40
0 10 20 30 40 50 60 70 80 90 100
Sh
eet
ash
co
nte
nt
(%)
Cumulative % of sheet from bottom to top
Baseline 25,1% Ash Bonding & Aggregation 28,8% Ash
Poly. (Baseline 25,1% Ash) Poly. (Bonding & Aggregation 28,8% Ash)
35 • Confidential and proprietary.
Grade
Furnish
Process
System Closure
Strength Program
Filler pre-treatment
Broke Pre-Treatment
Stock Pre-Treatment
Injection & Mixing
Retention Program
36 • Confidential and proprietary.