Indorama Ventures Public Co. Ltd. · SET:IVL

Indorama Ventures Public — Indorama Ventures — Technical Presentation (June 2024)

62 slides from Indorama Ventures Public's technical presentation, Jun 20, 2024

  1. Slide 1: Surfactants for Emulsion Polymerization

    Surfactants for Emulsion Polymerization Presented by Bruno Dario June 20th, 2024

  2. Slide 2: Agenda

    AGENDA Surfactants for Emulsion Polymerization 1. Indorama Ventures 2. Origin and Sustainability 3. Polymers and Process 4. Stability and Surfactants 5. Case Studies 6. Quick Guide: Transition to APE-free 7. Q&A © Indorama Ventures 2024 2

  3. Slide 3: Our Purpose

    OUR PURPOSE We enhance our relationships Reimagining Chemistry Together to Create A Better World Constant Value creation search for through innovation sustainability Purpose word choice explanation: Why we exist

  4. Slide 4: Over the last 20 years, IVL has acquired

    One of the world's leading producers of PET with Over the last Presence in Combined PET* 20 years, IVL 35 countries Global leader in the production of PET and r-PET has acquired Consolidated revenues of *Combined PET - Feedstock, PTA, PET, Packaging and Recycling FIBERS and US$ 18.7 bi Polyester fib

  5. Slide 5: Where We Are

    Integrated Oxides & Derivatives Where WE ARE Where WHERE WEwe AREare EMEA AMERICAS • Belgium • Brazil APAC • Mexico • United States • Australia • Uruguay • China • India 18 industrial units 8 countries 9 R&D centers 3,700 employees Indovinya Indovinya R&D Industrial facilities Units © Indorama Ventu

  6. Slide 6: Origin and Sustainability

    Origin and Sustainability Emulsion Polymerization © Indorama Ventures 2024 6

  7. Slide 7: Definitions

    Definitions When we talk about EMULSION POLYMERIZATION it is important to remember that… EMULSION AS WE POLYMERIZE SO, TODAY • Liquid dispersed in another liquid • Monomers will create a polymer, You will hear me talking about: • E.g., Mayonnaise which is a solid stabilized in water. A DISPERSION or

  8. Slide 8: Origins and Importance

    Origins and Importance Emulsion Polymerization World War II – shortage of natural rubber • Solution: free radical polymerization Versatility • Several types of polymers that can be made • Wide variety of applications Advantages: • Remove the heat of polymerization • High control of particle size and

  9. Slide 9: Sustainability Key Drivers

    Sustainability Key Drivers CASE Market Reduce environmental Efficient use of Enhance durability and social impact resources of materials Reduce VOC emissions Energy efficiency in Enhance short & long-term production processes performance Biobased alternatives High performance in HSE friendly formula

  10. Slide 10: Polymers and Process

    Polymers Click to edit andMaster title style Process Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 10

  11. Slide 11: General Formulation

    General Formulation Emulsion Polymerization % Weight Ingredients Minimum Maximum Water 50.0 55.0 Surfactant 0.5 5.0 Monomer 40.0 50.0 Initiator 0.2 0.5 © Indorama Ventures 2024 11

  12. Slide 12: Typical Monomers

    Typical Monomers Emulsion Polymerization Monomer Tg (°C) Affinity for Water 2-Ethylhexyl acrylate -64 Hydrophobic N-butyl acrylate -54 Hydrophobic Methyl acrylate 8 Hydrophobic Vinyl acetate 32 Hydrophilic Styrene 100 Hydrophobic Methyl methacrylate 106 Hydrophilic © Indorama Ventures 2024 12

  13. Slide 13: Application and Tg

    Application and Tg Acrylic polymers POWDER COATINGS INDUSTRIAL COATINGS ARCHITECTURAL COATINGS SELANTS (CAULKS) ELASTOMERIC COATINGS PSA - 50 °C - 25 °C 0 °C 25 °C 50 °C 75 °C 100 °C - 58 °F - 13 °F 32 °F 77 °F 122 °F 167 °F 212 °F © Indorama Ventures 2024 13

  14. Slide 14: Common Polymers applied in Architectural/Industrial Coatings

    Common Polymers applied in Architectural/Industrial Coatings Styrene-acrylic Vinyl-acrylic All-acrylic • Excellent hydrophobicity • Low-VOC capable (hydroplasticization) • Premium resins • Excellent adhesion to • Good scrub resistance • Excellent durability / weatherability metal/plastic • Good bala

  15. Slide 15: Diverting a little bit from the topic…

    Diverting a little bit from the topic… How do acrylics compare to other polymers applied in Architectural / Industrial Coatings? Chemical Resin UV Resistance Hardness Flexibility Heat Resistance Cost Resistance Air Dry Alkyd G to VG P to G G to VG P to G P to G VG to E Alkyd Melamine G to VG G to VG

  16. Slide 16: Emulsion Polymerization

    Emulsion Polymerization Simplified setup All-Acrylic Recipe Example 1. Prepare Initial charge and add to the reactor. 2. Heat up the reactor to 80-85°C under N2 atmosphere. 3. Charge 5 wt.% of Monomer Pre-emulsion in the reactor. 4. After this, add the First Initiator Batch in the reactor. 5. Keep t

  17. Slide 17: Parameters and Properties of Emulsion Polymers

    Parameters and Properties of Emulsion Polymers Emulsion Polymerization Common Process Issues Emulsion Polymer Properties • Clot dispersed in the latex • Residual Monomer • Polymer buildup on reactor surface • pH • Conversion time • Solid Content • … • Particle Size • Viscosity • Molecular Weight • T

  18. Slide 18: Stability and Surfactants

    Stability Click to edit andMaster title style Surfactants Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 18

  19. Slide 19: Colloidal Stability

    Colloidal Stability All- Acrylic < Styrene Acrylic Source: M. El-Aasser and P. Lovell, Emulsion Polymerization and Emulsion Polymers, Wiley, West Sussex, 1997 © Indorama Ventures 2024 19

  20. Slide 20: Surfactants – Surface Active Agents

    Surfactants – SURFACE ACTIVE AGENTS Anionic Charged Cationic Hydrophilic Polar Head (Affinity with water) Neutral Aromatic Hydrophobic Nonpolar Tail (No affinity with water) Aliphatic *Linear or Branched © Indorama Ventures 2024 20

  21. Slide 21: Alkylphenol Ethoxylate

    When talking about surfactants... The most “famous” one: Alkylphenol Ethoxylate Hydrophobe Hydrophile n • Polarizable Aromatic Ring • Dense electronic cloud • Creates a soft transition from hydrophobic to hydrophilic © Indorama Ventures 2024 21

  22. Slide 22: Anionic Surfactants

    Anionic Surfactants (A) Function: • Monomer emulsification • Particle Nucleation (B) Nc ∝ [Surfactant]0.6 • Polymerization speed • Particle size distribution • Clot formation • Shelf-life stability • Sensitive to salt concentration (C) (A) Sodium salt of sulfated lauryl alcohol (D) (B) Sodium dodecy

  23. Slide 23: APE-free Anionic Surfactants

    APE-free Anionic Surfactants Tailoring surfactants to fit our customer’s needs OXIMULSION® OXIMULSION® OXIMULSION® PROPERTIES 1228 1328 APH 11230 (A) EO Content* Low Low Medium Appearance Liquid Liquid Liquid Solids, wt.% 28 28 28 CMC, g/L 0.27 0.28 0.34 (B) S.T., 0.1%, 35 38 46 mN/m (A) sodium salt

  24. Slide 24: Nonionic Surfactants

    Nonionic Surfactants H3C O H O n 40n= 9 - 40 n= 9 - 40 CH3 Function • Electrolytic Stability • Stability during neutralization • Mechanical Stability • Freeze-thaw Stability • Shelf-life Higher steric repulsion is obtained when: • Thick and dense layers • Strong adsorption • Complete coverage © Indo

  25. Slide 25: APE-free Nonionic Surfactants

    APE-free Nonionic Surfactants Tailoring surfactants to fit our customer’s needs Hydrophobe Type Size Structure Distribution Sourcing • Fatty Alcohols • EO • Synthetic • # of Carbons • Linear • Broad range • Natural • PO Alcohols • EO units • Branched • Narrow range • Synthetic • EO/PO • Sorbitan est

  26. Slide 26: Alcohol Ethoxylates: Degree of Ethoxylation

    Alcohol Ethoxylates Tailoring surfactants to fit our customer’s needs Branched 40 C13 O/W Emulsifier C10 High Steric Repulsion Degree of Ethoxylation 20 2-PH Branching C13 – C15 12 High Surface Activity C11 6 C9 – C11 3 Cetearyl Stearyl Alcohol Alcohol Oil Soluble Lauryl Alcohol Linear 1 10 11 12 13

  27. Slide 27: Alcohol Ethoxylates: Branching

    Alcohol Ethoxylates Tailoring surfactants to fit our customer’s needs Branched C13 C10 Lower Cloud Points Better Handling Better Wetting Odor 2-PH Branching Better Emulsification Lower Odor C13 – C15 Lower Solidification Point Good Handling Longer solubilization Time Good Wetting C11 Good Emulsifica

  28. Slide 28: What to consider when choosing surfactants

    What to consider when choosing surfactants Performance Sustainability Attributes • Clot Formation ↑ BIODEGRADABILITY • Particle Size and Control during the ↓ TOXICITY process ↑ [Renewable Content] ↑ Electrolyte Stability ↑ Ease of processing / energy savings ↑ Mechanical Stability ↑ Water Resistance

  29. Slide 29: Anionic Surfactants

    Click to edit Master title style Anionic Surfactants Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 29

  30. Slide 30: Anionic Surfactants

    Anionic Surfactants OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® PROPERTIES 1228 1328 APH 11230 2742 Description Sulfated Sulfated Sulfated Phosphate EO content* Low Low Medium Low Appearance Liquid Liquid Liquid Liquid Solid Content, wt.% 28 28 28 > 95 Solvent Water Water Water Water pH 7 11 8 3

  31. Slide 31: Two Step Process

    Two Step Process Emulsion Polymerization 1° STEP | Generation of Seeds MONOMERS Anionic Surfactant SC ~ 10 wt% < 50 nm 2° STEP | Growth of Seeds MONOMERS Anionic Surfactant 1018 seeds/L SC ~ 50 wt% < 200 nm Source: Asua et. Al., Langmuir 2003, 19, 3212 - 3221. © Indorama Ventures 2024 31

  32. Slide 32: Formulations: Two Step Process

    Formulations Emulsion Polymerization Two Step Process Components (phm) Step 1 Step 2 Methyl methacrylate 50 50 Butyl acrylate 48 48 Methacrylic acid 1 1 APE-free anionic surfactant 25 2 Buffer 0.7 0.7 • Thermal initiator: 4h at 80 °C Ammonium persulfate 0.6 0.6 • Redox initiator: 1h at 60 °C Oxidizi

  33. Slide 33: Formulations: Seeded Process

    Formulations Emulsion Polymerization Seeded Process OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® Properties Benchmark 1228 1328 APH 11230 2742 Solid Content, wt.% 50 50 50 50 50 pH 9 9 9 9 9 Viscosity, 25°C, cP 300 281 235 186 185 Zeta Potential, mV -77 -60 -59 -58 -56 Freeze-thaw stability (Cycl

  34. Slide 34: Effect of surfactant on coagulum formation

    Effect of surfactant on coagulum formation in the reactor 1000 200 170 173 800 150 155 148 Particle Size (nm) Filterable Soids (ppm) 150 600 100 400 331 200 50 0 0 0 0 OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® 0 1228 1328 APH 11230 2742 Benchmark OXIMULSION®OXIMULSION®OXIMULSION®OXIMULSION® 12

  35. Slide 35: Effect of surfactant on mechanical stability

    Effect of surfactant on mechanical stability 3000 60 CaCl2 Concentration (mmol.L-1) Filterable Solids (ppm) 2000 40 2000 28 20 1000 12 0 0 0 51 45 46 25 0 0 Benchmark OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® Benchmark OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® 1228 1328 APH 11230 2742 12

  36. Slide 36: Effect of surfactant on wet scrub resistance

    Effect of surfactant on wet scrub resistance of 30% PVC paint Emulsion Polymerization ASTM D2486 800 726 Number of Cycles 700 672 651 628 600 569 500 400 Benchmark OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® 1228 1328 APH 11230 2742 © Indorama Ventures 2024 36

  37. Slide 37: Effect of surfactant on blocking and dirt pickup

    Effect of surfactant on blocking evolution of 30% PVC paint Dirt Pickup ASTM D4946 Rating: 1-11 / (1=Best) 10 12 11 10 8 10 8 8 6 Grade Grade 4 4 4 6 4 3 4 4 3 2 2 2 2 2 2 2 2 2 2 2 1 2 0 0 Benchmark OXIMULSION® OXIMULSION® OXIMULSION® OXIMULSION® Benchmark OXIMULSION® OXIMULSION® OXIMULSION® OXIMUL

  38. Slide 38: Nonionic Surfactants

    Click to edit Master title style Surfactants Nonionic Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 38

  39. Slide 39: Vinyl-Acrylic Emulsion

    Vinyl-Acrylic Emulsion SURFONIC® NB-407 OXITIVE® 7110 OXITIVE® 7140 Physical-Chemical Properties Physical-Chemical Properties Physical-Chemical Properties • Nonylphenol ethoxylated • Fatty alcohol ethoxylated • Synthetic alcohol ethoxylated • 40 EO • Medium degree of ethoxylation • High degree of et

  40. Slide 40: Vinyl-Acrylic Emulsion

    Vinyl-Acrylic Emulsion SURFONIC® NB–407 OXITIVE® 7110 OXITIVE® 7140 Components Weight (%) Components Weight (%) Components Weight (%) Initial Charge Initial Charge Initial Charge Water 34.6 Water 34.6 Water 34.5 0.2 Buffer 0.2 Buffer 0.2 Buffer HEC HEC 0.2 HEC 0.2 0.2 ® ALKOPON® NNP 940 HS 0.2 OXIMU

  41. Slide 41: Total Filterable Solids

    Effect of different nonionic surfactants Reactor Cleanliness 500 410 400 • Clot formation < 500 ppm for Total Filterable Solids (ppm) all formulations. 300 224 200 • Longer ethylene oxide chain in the nonionic improved the 98 100 performance even compared against reference. 0 NP-4EO-SNP-40EO / NP-40

  42. Slide 42: Average Particle Size

    Effect of different nonionic surfactants Particle Size 450 400 379 • Acceptable particle size range is 200 350 – 400nm. Average Particle Size (nm) 300 250 208 • Longer ethylene oxide chain 190 200 in the nonionic surfactant 150 tends to decrease the particle size. 100 50 0 ® ® NP-4EO-S /NP-40EO NP-4

  43. Slide 43: Mechanical Stability

    Effect of different nonionic surfactants Mechanical Stability 6000 5000 4396 Mechanical Stability (ppm) 4000 2795 3000 • Longer EO chain in the 2000 1600 nonionic improved the mechanical stability; 1000 0 NP-4EO-SNP-40EO / NP-40EO (5:95) L2S / L20®(5:95) OXITIVE 7110 L2S / B40®(5:95) OXITIVE 7140 ©

  44. Slide 44: Emulsion Polymer Formulation

    Emulsion Polymer Formulation Goal: to evaluate different ratios of nonionic to anionic surfactants: 95:5 / 85:15 Monomer Mix Initiator Components (phm) Formulation 1 4.0h 4.5h Vinyl Acetate 80 % Butyl acrylate 20 % Active Content (phm) OXITIVE® 7110 3.74 – 4.18 OXIMULSION® 1228 0.22 – 0.66 Upfront C

  45. Slide 45: Total Filterable Solids

    Effect of different ratios of nonionic to anionic Reactor Cleanliness 500 410 400 • Clot formation < 500 Total Filterable Solids (ppm) 300 ppm for all formulations. 224 200 158 • New ratio of anionic to nonionic reduced clot formation. 100 0 ® ® NP-4EO-S NP-4EO-S / (5:95) / NP-40EO OXIMULSION 1228 /

  46. Slide 46: Average Particle Size

    Effect of different ratios of nonionic to anionic Particle Size 450 400 379 382 350 • Acceptable particle size range Average Particle Size (nm) 300 is 200 – 400nm. 250 200 190 150 • Low impact in particle size. 100 50 0 NP-4EO-S ® NP-4EO-S / NP-40EO/ (5:95) OXIMULSION L2S / L20 (5:95)1228 / ® L2S /

  47. Slide 47: Mechanical Stability

    Effect of different ratios of nonionic to anionic Mechanical Stability 6000 5000 4396 • Less than 1.0% clot formed Mechanical Stability (ppm) 4000 under shear stress. 3000 2598 • New ratio of anionic to nonionic reduced clot formation after 2000 1600 mechanical stress. 1000 0 ® ® NP-4EO-SNP-4EO-S /

  48. Slide 48: Wet Scrub Resistance

    Vinyl-Acrylic Paint Scrub Resistance – ASTM D2486 7000 6000 6000 5260 Wet Scrub Resistance (cycles) 5000 4233 3564 4000 2609 3000 1996 2000 1000 0 ® BENCHMARK Benchmark BENCHMARK Latex APE BENCHMARK LATEX Benchmark Latex APE- NP-4EO S / NP-40EO NP-4EO-S NP-40EO OXIMULSION 1228 / L2S / L20 (5:95) L2S

  49. Slide 49: Reactive Surfactants

    Click to edit Master title styleSurfactants Reactive Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 49

  50. Slide 50: Why does it happen?

    Why does it happen? LATEX Fragile Film STAGE I T>MFFT Continuous and STAGE II Transparent Film T>Tg STAGE III Coalesced Film © Indorama Ventures 2024 50

  51. Slide 51: OXIMULSION REACT N1

    OXIMULSION REACT® N1 H2C [ ]m A [ O ] O n H APEO-free Partially Bio- Concentrated Product VOC ≤ 5 g/L based Solid content >99 wt.% Air Water Liquid HLB of 15 Behave as conventional Compatible with surfactants all latexes © Indorama Ventures 2024 51

  52. Slide 52: Two Step Process

    Two Step Process Emulsion Polymerization 1° STEP | Generation of Seeds MONOMERS O O – S + H3C O O Na SC ~ 10 wt% n O 40 - 50 nm 2° STEP | Growth of Seeds MONOMERS O H H2C A O m n O O – S + H3C O O Na SC ~ 45 - 50 wt% 1018 seeds/L n O ~ 100 nm Source: Asua et. Al., Langmuir 2003, 19, 3212 - 3221. © I

  53. Slide 53: Emulsion Polymerization Starting Formulations

    Emulsion Polymerization Starting Formulations Components w/w Methylmethacrylate (MMA) 0.75 SEEDED SEMI-BATCH PROCESS Butyl acrylate (BA) 0.72 Latex seed (Previously Methacrylic acid 0.03 prepared) Anionic surfactant* 0.38 Ammonium persulfate 0.004 Methylmethacrylate (MMA) 23 Butyl acrylate (BA) 22 P

  54. Slide 54: Effect of Surfactant Composition on Coagulum Formation

    Effect of Surfactant Composition on Coagulum Formation in EP 75 wt% REACT® N1 67 wt% REACT® N1 50 wt% REACT® N1 25 wt% Anionic Surfactant 33 wt% Anionic Surfactant 50 wt% Anionic Surfactant Coagulum in Reactor Thermocouple C Impeller Dispersed coagulum in 800 ppm 834 ppm 805 ppm latex © Indorama Ven

  55. Slide 55: Incorporation of Reactive Nonionic Surfactant

    Incorporation of Reactive Nonionic Surfactant Surfactant Incorporation = Total Surfactant - Free Surfactant 120 100 100 Incorporation (wt%) 80 60 40 20 0 0 2 phm AS 1 phm AS + 1 phm REACT N1 © Indorama Ventures 2024 55

  56. Slide 56: Water Absorption

    Water Absorption Latex films with 2 phm of coalescent immersed in water at 25°C Commercial AS/REACT N1 AS 100 WATER ABSORPTION (WT%) 80 60 40 20 0 0 5 10 15 20 25 30 IMMERSION TIME (DAYS) © Indorama Ventures 2024 56

  57. Slide 57: Whitening

    WHITENING Latex films with 2 phm of coalescent immersed in water at 25°C after 4 days Commercial AS / REACT® N1 (1:1) © Indorama Ventures 2024 57

  58. Slide 58: Transition to APE-free Surfactants

    Transition Click to edit toMaster APE- title Surfactants free style Click to edit Emulsion Polymerization Master subtitle style © Indorama Ventures 2024 58

  59. Slide 59: APE-FREE Alternatives to APE-based Nonionic Surfactants

    APE-FREE Alternatives to APE-based Nonionic Surfactants Emulsion Polymerization APE-FREE HLB APE-based Nonionic HLB Alternatives OXITIVE® 7254 13.4 SURFONIC® N-95 13.1 OXITIVE® 7110 16.9 SURFONIC® NB-307 17.1 OXITIVE® 7130 17.4 SURFONIC® NB-307 17.1 OXITIVE® 7140 18.0 SURFONIC® NB-407 17.8 OXITIVE®

  60. Slide 60: Replacement of APE-based for APE-FREE Surfactants

    Replacement of APE-based for APE-FREE Surfactants Emulsion Polymerization Replacement of APE for APE-FREE Surfactants in Styrene-Acrylic Latex APE-based APE-free solution Replacement of APE for APE-FREE Surfactants in Vinyl-Acrylic Latex OXIMULSION® B1000 NP 9.5 EO SULFATED + NP 23 EO APE-based APE-

  61. Slide 61: Q&A Session

    Q&A Session Surfactants for Emulsion Polymerization Contact Click to edit Master Bruno Dario title style Research Scientist II – CASE & Performance Products +1 (346) 413-1152 (mobile) Click to edit Master subtitle style bruno.dario@us.indorama.net Indorama Ventures – Indovinya 8401 New Trails Dr., S

  62. Slide 62: Disclaimer

    Disclaimer This presentation and its content (“Material”) is proprietary to Indorama Ventures Public Company Limited (“Indorama Ventures”) and/or its affiliates (collectively, the “Group”) and may not be, in whole or in part, reproduced or disclosed, published, distributed or released to any other p

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