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TRANSCRIPT
17. February 2014
Frank Neuber
Applications & Development Manager - NORAM
Additives Masterbatches BU Clariant Corporation
INNOVATION TAKES ROOT 2014
Utilizing HYDROCEROL™Chemical Foaming Agents to Reduce Density and Material Cost in PLA Sheet for Thermo-formables
CONTENTS
1) Clariant Corporation Introduction
2) Why Reduce Density - Economic Benefits of Density/Material Reduction Explained
3) How to Achieve Density Reduction - Chemical Foaming Agents (CFA’s) Explained
4) Keeping the Best Structure and Physicals – CESA-extend Explained
5) Comparative Examples from Clariant EU and NORAM
6) Summary and Conclusions
7) Citations & References
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1) CLARIANT : A world leader in specialty chemicals
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Clariant focuses on creating value by investing in future profitable and sustainable growth.
KEY FACTSSales 2012 (CHF m)
6 038
More than
100Group companies worldwide
EBITDA 2012 (CHF m)before exceptionals
802
End 2012
~21 202employees
Represented in
76countries worldwide
7Business Units
(incl. discontinued operations)
CLARIANT MASTERBATCHES
MasterbatchesClariant Masterbatches is the leading manufacturer of colorand additive concentrates and technical compounds for the plastics industry; supplying the packaging, consumer goods, medical, textile and automotive industries.
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2) Returning to the subject…Why Reduce Density ?
Economics. The same article made with less material is more economically attractive.
Example: 40 thermoformed PLA trays (from sheet) weigh a pound (454g), and these can now be made using 20% less PLA
This PLA application can yield a net savings of ~ $165,000 per each $1MM of PLA.
Or,… make 20% more sheet with same amount of PLA.
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Cost Savings Explained from Foaming PLA (from Clariant’s CFA Value Calculator)
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Value Units Value
Resin Cost $USD per pound $1.00
Resin Specific Gravity grams per cubic centimeter 1.24
Hydrocerol CFA Cost $USD per pound $3.50
Hydrocerol CFA Dose Percent 1.0%
Density Reduction Percent 20.0%
Annual Volume of Resin Processed Pounds 1,000,000
As-Is With HYDROCEROL
Annual Volume of Resin Processed 1,000,000 800,000
Annual Volume of HYDROCEROL Processed 0 10,000
Annual Resin Cost $1,000,000 $800,000
Annual HYDROCEROL Cost $35,000
TOTAL Annual Material Cost $1,000,000 $835,000
Annual Net Savings with HYDROCEROL $165,000
Cost Savings Achievable with Foam PLA - continued
(from Clariant’s CFA Value Calculator)
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Hydrocerol Price =========> $ 3.50 Hydrocerol Dose =====> 1.00% Starting Resin Price ==> $ 1.00
Density Reduction Percent RESIN COST PER POUND
$ 0.88 $ 0.90 $ 0.92 $ 0.94 $ 0.96 $ 0.98 $ 1.00 $ 1.02 $ 1.04 $ 1.06 $ 1.08 $ 1.10 $ 1.12 $ 1.14
12% Savings per pound ==> $0.079 $0.082 $0.085 $0.087 $0.090 $0.092 $0.095 $0.098 $0.100 $0.103 $0.105 $0.108 $0.111 $0.113
14% Savings per pound ==> $0.097 $0.100 $0.103 $0.106 $0.109 $0.112 $0.115 $0.118 $0.121 $0.124 $0.127 $0.130 $0.133 $0.136
16% Savings per pound ==> $0.115 $0.118 $0.121 $0.125 $0.128 $0.132 $0.135 $0.138 $0.142 $0.145 $0.149 $0.152 $0.155 $0.159
18% Savings per pound ==> $0.132 $0.136 $0.140 $0.144 $0.147 $0.151 $0.155 $0.159 $0.163 $0.166 $0.170 $0.174 $0.178 $0.182
20% Savings per pound $0.150 $0.154 $0.158 $0.162 $0.167 $0.171 $0.175 $0.179 $0.183 $0.188 $0.192 $0.196 $0.200 $0.204
22% Savings per pound ==> $0.167 $0.172 $0.177 $0.181 $0.186 $0.190 $0.195 $0.200 $0.204 $0.209 $0.213 $0.218 $0.223 $0.227
24% Savings per pound ==> $0.185 $0.190 $0.195 $0.200 $0.205 $0.210 $0.215 $0.220 $0.225 $0.230 $0.235 $0.240 $0.245 $0.250
26% Savings per pound ==> $0.203 $0.208 $0.213 $0.219 $0.224 $0.230 $0.235 $0.240 $0.246 $0.251 $0.257 $0.262 $0.267 $0.273
28% Savings per pound ==> $0.220 $0.226 $0.232 $0.238 $0.243 $0.249 $0.255 $0.261 $0.267 $0.272 $0.278 $0.284 $0.290 $0.296
30% Savings per pound ==> $0.238 $0.244 $0.250 $0.256 $0.263 $0.269 $0.275 $0.281 $0.287 $0.294 $0.300 $0.306 $0.312 $0.318
($0.050)
$0.000
$0.050
$0.100
$0.150
$0.200
$0.250
$0.300
$0.350
12% 14% 16% 18% 20% 22% 24% 26% 28% 30%
Savi
ngs
per P
ound
Percent Weight ReductionN S i
3) How to Achieve Density Reductions? CFA
“..♫.tiny bubbles ”
Explained: Chemical foaming agents (CFA’s) release gasses (CO2 for PLA) which displace polymer, forming a microscopic foam structure.
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Common Endothermic CFA’s explained:
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What about the water produced...in a polyester?
– Clariant has formulated its Hydrocerol CFA’s with water and Lewis acid scavengers to capture the water generated from common endothermic CFA ingredients, which can hydrolyzea polyester [read PLA].
– These advancements have allowed us to apply Hydrocerol CFA’s in previously “off limit” applications, such as thin films, thin trays, trays needing cold impact integrity, etc.
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Hydrocerol CFA’s…..We’ve Evolved.
Early attempts 2008 attempts Current Accomplishments
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4) Keeping the Best Physicals - How we do it
Trade secret, of course, but we can share a few details, below:
1) Improved PLA integrity; i.e. HDT, m.w. retention, gas cell nucleation, etc.
2) Developed the process to optimize the reaction, gas capture and laminar
flow needed when changing the polymer viscosity and apparent density.
3) Controlled the typical hydrolysis effects on polyesters, from using endo-
thermic CFA’s; i.e. scavenged released moisture and repaired hydrolyzed
and sheared PLA chains, increasing their melt strength and ability to form
the cellular structure. Using Clariant’s patented CESA-extend™ (CE)
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CE Rebuilds Polymers
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“ HOW
DOES IT
DO THAT ?”
CE Chemistry14
“I will explain.”
CESA®-extend is a multi-functional, oligomeric material:
- Very high epoxy functionality
- Unique mix of functionalities to maximize chain end-group branching without cross-linking or gel formation
- Rejoins cleaved ends to increase the molecular weight and melt strength
The great John Houseman from the movie The Paperchase
Extender in Hydrolyzed and Sheared Polyesters15
CE epoxy-functionality
Sheared or HydrolyzedPolyester lower m.w. chains
Higher m.w. Polyester Final product
5) Early Example- Unprotected Foaming
– 1% Hydrocerol CT3108
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Improved Examples - Protected Polymer Foaming
– 1% Hydrocerol CT 3108 + 1% CESA-extend
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Side–by–Side Comparison of Structures – EU Foam
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Unprotected Protected
Some Notable EU Machine and Energy Efficiencies
– Hydrocerol CFA alone dropped Head PSI to 2675 (from 3260 standard)
– Hydrocerol + Extender increased Head PSI to 3100 (viscosity increase)
– Amp load decreased to 28 (from 31 for standard Non-foamed) = 9.67% red.
- Foam Melt Temperatures = 178.4 F (versus Standard of 186.1 F)
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North American Developmental Results
– Pushed the Density reduction in mono-layer sheet to 28%
– Tri-Layer sheet (20:60:20) with up to 18% total density reduction (i.e. 30% density/material reduction in centerlayer) matches un-foamed standard sheets of same thickness for surface and impact physicals
– Proceeding with major select OEM’s per above-stated
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Example– NORAM Developments in 0.65mm sheet
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Example NORAM Developments in 0.65 mm PLA sheet
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Foamed Articles made with PLA
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Supporting Data:Density Reduction* vs. Hydrocerol Dose
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CFA% Avg. Density
STD PLA 0 1.2504
CFA 8607 Only 1 0.9966
CFA 8607 + 0.8%493 1 1.0819
CFA 8607 + 0.8%493 1.5 1.0085
CFA 8607 + 0.8%493 2 0.8972
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.5 1 1.5 2 2.5
Density(g/cc)
% Hydrocerol 8607 (with 0.8% Extender 493)
** Density determined by both Archimedes Principle Method and He displacement pycnometry
Supporting Data – MFR** with Hydrocerol and CE
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CFA%
MFR (210C,2.16Kg),(g/10Min.)
STD PLA 0 6.7
CFA 8607 Only 1 26.2
CFA 8607 + 0.8%493 1 16.5
CFA 8607 + 0.8%493 1.5 17.8
CFA 8607 + 0.8%493 2 21.9
0
5
10
15
20
25
30
1 2 3 4 5
CFA%
MFR(210C,2.16Kg),(g/10Min.)
**MFR determined on Tinius Olsen Melt Indexer
6) Summary & Conclusions:
PLA may be foamed to reduce density / material cost, with Additives which have FDA compliancy for Indirect Food Contact
The process conditions which allow its optimization are critical to success: temperatures, pressures, cooling, etc.
Extender technology rebuilds PLA melt strength and allows greater density reductions while maintaining physicals
Competitive economies versus “traditional” polymers like PS may be achieved with Hydrocerol CFA and CESA-extend technology in PLA.
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7) Citations & References:– [1] Wiesner, Müller: “The right Chemical Foaming Agent for your Application” 6th
International Conference, Blowing Agents and Foaming Processes, May 2004, Hamburg, Germany
– [2] Lübke, Wiesner: “Developments of New High Temperature Chemical Foaming Agents”, 4th International Conference, Blowing Agents and Foaming Processes, May 27 – 28, 2002 in Heidelberg / Germany
– [3] Wegner, J.: “Additives for foamed sheets” Kunststoffe 1/2005, Carl Hanser Verlag,
– [4] Groeseling, Mirko: ”Chain extender – brancher for polyester”, Clariant internal presentation, 9/2001
– [5] Villalobos, Marco; Awojulu, Abiodon; Turco, Gregory: “The Process of Recycling of Polyesters with Polymeric Chain Extenders”, published in Polymer Science and Engineering, Feb. 21, 2005
– [6] Pilla, Srikanth; Kim, Seong G.; Auer, George K.; Gong, Shaoquin; Park, Chul: “Microcellular Extrusion Foaming of Polylactide with Chain Extender” published in Polymer Science and Engineering, Aug. 1, 2009
– [7] Keefe, Lawrence; Hydrocerol CFA Savings Calculator; Clariant MasterbatchesLLC, public interactive document, published in Winchester, VA, Feb. 1, 2013
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QUESTIONS ?