Chromate free surface pre-treatments for aluminium alloys. ASETSDefense Martin Beneke Sonja Nixon

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ASETSDefense Martin Beneke Sonja Nixon Chromate free surface pre-treatments for aluminium alloys

Drivers for chromate replacement Airbus Environmental aims: Remove hazardous (CMR) substances from a/c and plants Airbus ACF (Airbus Chromate Free) program started in 2002 REACH regulation: Registration, Evaluation, Authorisation and Restriction of Chemicals CrO 3, official REACH sunset date: 9/2017 CrO 3 is used e.g. for CAA, CrVI CCC, Acidic Pickling processes, Hard Chrome plating, etc. CTAC: Chromium Trioxide Authorization Consortium Aim: Use of CrO 3 after the sunset date RAC and SECA recommendation for final decision of European Commission: CrO 3 banned and full implementation of replacements in manufacturing and supply chain latest end 9/2024 necessary!

Surface pre-treatment of aluminium alloys Potential Chromate containing processes / products Anodising Painted / Paint Primer Sealing, unpainted Bonding Primer Degreasing Alkaline Treatments Acidic Treatments Chemical Conversion Coating Painted / Paint Primer Unpainted Topics discussed in this presentation Wash Primer Other processes Painted / Paint Primer DPI Welding: LBW, FSW Chemical milling

Anodising CAA Replacement TSA anodising Application of bonding primer CAA Cr VI 1:1 Replacement solution Painted parts Corrosion Protection TSA Unpainted parts n/a Structural Bonding PSA Basic Primer Application, Unsealed TSA plus Post Treatment, Sealing Process Bonding Primer Chromate free CCC options are available CAA: Chromic Acid Anodising TSA: Tartaric Sulphuric Acid Anodising PSA: Phosphoric Sulphuric Acid Anodising CCC: Chemical Conversion Coating

CAA replacement: TSA Anodic Pre-treatment (2006) Tartaric Sulphuric Acid Anodising compared to CAA eco-efficient alternative to CAA fulfilling the same requirements TSA is standard for A350 (CAA was only temporarily accepted) 120 Supplier world wide qualified to TSA AIPS 02-01-003 10 years manufacturing experience with time reduction by ~ 30% TSA anodic film CAA key process parameter Film thickness 2-5 µm Alkaline Cleaning Acidic Treatments Alkaline Etching Acidic Treatments TSA key process parameter Film thickness 2 7 µm Temperature Process time 40 C 45 min Rinsing Rinsing Temperature Process time 37 43 C 20 25 min Voltage Chromic Acid content 40 V or 21 V 30-100 g/l CAA TSA Voltage Tartaric Acid content 13 15 V 80 g/l Rinsing Rinsing Sulphuric Acid content 40 g/l

TSA process development Morphology and thickness dependence in relation to TSA process parameters B13 B23 B33 B43 B53 CAA Sample Alloy Process parameter Oxid thickness B13 2024 bare 13V; 5+20min; 37 C 1.8 µm B23 2024 bare 15V; 5+30min; 37 C 3.1 µm B33 2024 bare 15V; 5+20min; 43 C 3.2 µm B43 2024 bare 18V; 5+30min; 43 C 4.6 µm B53 2024 bare 13V; 5+25min; 50 C 5.0 µm CAA 2024 bare 3.3 µm

TSA development in relation to Adhesion and FFT results Airbus CrVI based EP Primer Adhesion Filiform Corrosion Sample Alloy Anodizing Process (TSA) Oxide Film thickness GT after 0h GT after 168h H2O Max [mm] Average of 5 Fila [mm] B12 2024 bare 13V; 5+20 min; 37 C 1,8µm 1 0 3 1,4 B15 2024 bare 13V; 5+20 min; 37 C 1,8µm 0 1 4 2,7 B22 2024 bare 15V; 5+30min; 37 C 3,1 µm 1 1 1,5 1,2 B25 2024 bare 15V; 5+30min; 37 C 3,1 µm 1 1 1,5 1 B32 2024 bare 15V; 5+20min; 43 C 3,2 µm 0 0 1 0,7 B35 2024 bare 15V; 5+20min; 43 C 3,2 µm 0 0 2 1,5 B42 2024 bare 18V; 5+30min; 43 C 4,6 µm 0 0 0,5 0,5 B45 2024 bare 18V; 5+30min; 43 C 4,6 µm 0 0 1 1 B52 2024 bare 13V; 5+25min; 50 C 5 µm 1 0 0,5 0,5 B55 2024 bare 13V; 5+25min; 50 C 5 µm 0 0 0,5 0,5 2024 bare CAA 3,3 µm 0 0 1,0 1,0 Wide TSA process window available TSA parameter selection was done in relation to TSA film and corrosion protection performance

Why TSA? Role of tartaric acid EIS results, currentless time in sulphuric acid and sulphuric/tartaric acid TEM investigation after dissolution experiments with tartaric acid Tartaric acid acts as an inhibitor and reduces e.g. the currentless dissolution of the TSA / anodic oxide film: Higher process robustness for manufacturing Constant and better corrosion protection performance

TSA chromate free sealing process CrIII/Zr CCC Sealing options: Chemical Conversion Coating, CrIII / Zr CCC process (TCP): E.g.: SurTec 650 (~ 20 %, 25 ~ 35 C, 5 ~ 10 min) TSA Al oxide Pores Sealing Layer Alu. alloy TSA anodising TSA Alu. alloy Barrier layer Sealing TSA Alu. alloy Barrier layer Sealing

TSA CrIII/Zr CCC sealing results TSA Standard Sealing Post-treatment Salt spray test AIPI 02-01-003 5 + 20 min SurTec 650 5 ~ 15 min 25 ~ 35 C Hot water sealing ISO 9227 336 h TSA long cycle Extended cycle 5 + 40 min ISO 9227 504h Results validated in shop trials are equivalent to M&P lab experience and meet the requirement of 336h SST For extended SST resistance (504h SST), modified TSA long cycle can be used as option Long cycle TSA plus 650 met 336h SST without hot water sealing

PSA: Anodising for structural bonding (2010) PSA Phosphoric Sulphuric Acid Anodising for bonded structures Anodising (PSA) Bonding Primer application Structural adhesive Basic primer application PSA Aluminium alloy Bonding primer Basic Primer Adhesive Painted surfaces Bonded structures

Passive Protection: PSA anodic Pre-treatment Phosphoric Sulphuric Acid Anodising (PSA) fulfils the same requirements as CAA in combination for bonding application substitution process for surface preparation prior to metal bonding reduced process time C red, Pimer lower voltage and bath temperature CAA CAA key process parameter PSA PSA key process parameter Film thickness 2-5 µm Film thickness 1-5 µm O blue (Al2O3) Temperature 40 C Temperature 26-28 C Process time 45 min Process time 23 min Voltage 40 V to 50 V Voltage 18 V Al alloy Chromic Acid content 30-100 g/l Phosphoric Acid content Sulphuric Acid content 110-125 g/l 75-80 g/l PSA is optimised for adhesion: Good penetration of the Bonding Primer into the PSA anodic oxide for good mechanical interlocking

Oxide growth Oxide growth Chromate free surface pre-treatments for aluminium alloys Passive Protection: PSA anodic Pre-treatment CAA PSA PSA 40 C PSA CAA 40 V 50 V 28 C 18 V 0 Cross section (TEM) 500 nm Top view (SEM) 45 min 23 min Cross section (TEM) 50023 nm min Top view (SEM)

PSA anodic Pre-treatment PSA and CAA fulfil the same requirements for adhesion, corrosion protection and fatigue according to AIPS 02-01-006 Anodic film properties Bondingprimer + Paint properties Bonding properties Fatigue properties Visual aspect Film thickness Morphology Film weight Salt spray test Crosscut test Dry Wet Filiform Salt spray test Adhesive peel test Bondline corrosion test Kt1.7 visual inspection by naked eyes SEM, ISO 2360 or ISO 1463 SEM EN 12373-2 ISO 9227 ISO 2409 EN 3665 ISO 9227 EN 1967 AITM 5-0009 EN 6072 and AIPS 02-01-001, AIPS 02-01-003, AIPS 02-01-006 PSA cannot be adequately sealed BC 300 days SST: <30% corrosion on 2024 clad

TSA / PSA industrial implementation from lab to production size Development (upscaling) 200 ltr 4 ltr M&P BRE 1.100 ltr 20.000 ltr IW SUR Manufacturing BRE Implementation Production 4.000 ltr Manufacturing Nordenham 20 m 3 30 m 3 84 m 3 125 m 3 300 m 3 already in production good experience since 2006 implementation in progress Minimize risk by starting TSA and PSA implementation in small galvanic lines

Chromate free conversion coatings Potential Technologies: Silane Sol-Gel Zr/Ti CCC Ce CCC TCP, CrIII/Zr technology Others: Mn, Mo, Best candidate today is the CrIII/Zr technology in relation to standard requirements, 168h SST, Paint adhesion and electrical conductivity. Lack of CrIII/Zr technology today: Process robustness SST performance at 168h limit or below Optical visibility / quality control Overall corrosion protection performance with chromate free paint schemes

Selected CrIII/Zr process: Basic reactions at the aluminium surface After several screening programs CrIII technology selected as best available technology for corrosion protection Dissolution of aluminium oxide layer, dissolution of aluminium Increase of ph at the metal/electrolyte interface Precipitation of Cr(OH) 3 and Zr(OH) 4 Crack formation, re-passivation of cracked area

Pickling Oxide Etched pickling Oxide Dense CCC film 1D CCC film cracks 2D CCC film cracks 3D CCC film cracks Chromate free surface pre-treatments for aluminium alloys CrIII CCC formation: Relation of Surface properties to SST performance SEM 9 4 5 6 7 8 Treatment time SST

Pickling Oxide Etched pickling Oxide Dense CCC film 1D CCC film cracks 2D CCC film cracks 3D CCC film cracks Chromate free surface pre-treatments for aluminium alloys CrIII/Zr CCC: OCP / SEM relation 9 4 5 6 7 8 Optimum painted corrosion protection Optimum bare SST corrosion OCP 2024 unclad (bath process example) Crack free layer formation between 3 to 5 minutes

Chemical Conversion Coating Process: Pretreatment options CCC process sequence SD Solvent Degreasing (optional) SD Solvent Degreasing (optional) AC Alkaline Cleaning AC Alkaline Cleaning AE Alkaline Etching AP Acidic Pickling AP Acidic Pickling Acidic Pickling oxide Surface CCC Chemical Conversion Coating Painted Parts Unpainted Parts Surface Preparation Final CCC treatment step Chromic Sulphuric Pickling solution already replaced by chromate free pickling solutions Chromates needs to be replaced for CCC

mv vs. SCE mv vs. SCE Chromate free surface pre-treatments for aluminium alloys Alloy influence, monitoring of oxide / MDL removal in surface treatment Open Circuit Potential (OCP) measurements in [F -, Fe 2+/3+, HNO 3 ] based Acidic Pickling solution on 2024 unclad 50 40 30 20 10 0 Applied Process: SD -> AC -> AE -> AP Alkaline degreasing, alkaline etching 0 2 4 6 8 10 12 14 t / min 20 C 25 C 30 C 35 C 40 C 60 50 40 30 20 10 0 Applied Process: SD -> AC -> AE -> AP Solvent degreasing -10 0 2 4 6 8 10 12 14 t / min For standard pre-treatment with AC and AE, Cu removal correlates with temperature to constant plateau within the specified time limits for pre-treatments In case of soft surface cleaning without alkaline etching, no plateau is reached within 15 minutes at 20 and 25 C in Acidic Pickling solution, indicating that the surface conditions are still dominated by residues of the rolling process 20 C 25 C 30 C 35 C 40 C

Impact of acidic pickling oxide on the CCC process OCP of Surtec 650 after 10 min acidic pickling in two solutions Red: F -, Fe 2+/3+, HNO 3 Black: Fe 2+/3+, HNO 3 /H 2 SO 4 168h SST result after 2 min treatment time

Pickling Oxide: [F -, Fe 2+/3+, HNO 3 ] etching solution OCP measured in CrIII CCC solution, Surtec ChromitAl 650 after 10 min acidic pickling in different [F -, Fe 2+/3+, HNO 3 ] solutions [F -, Fe 2+/3+, HNO 3 ] solution: [F -, Fe 2+/3+, HNO 3 ] solution: Conditions of [F -, Fe 2+/3+, HNO 3 ] Acidic Pickling solution are leading to a strong impact on the CCC process. No stable CCC parameter window Difficult to operate the CCC process on its optimum in relation to existing requirements!

CrIII/Zr plus PACS post treatment for performance improvement Substrate Surtec 650 Socomore TCS Somomore PACS sealing SST white pits SST white pits / sample Average pits per dm 2 per parameter XPS Cr spectra Surtec 650 Temp. Time Temp. Time Temp. Time 48h 168h 168h 2024 uc 23 2 OK 14; 6; 2 6,1 23 4 OK 13; 21; 22 15,6 23 6 OK 0; 0; 0 0,0 2024 uc 23 2 OK 9; 15; 18 11,7 23 4 OK 12; 6; 19 10,3 23 6 OK 55; 24; 26 29,2 2024 uc 23 2 23 5 min OK 0; 0; 0 0,0 23 4 23 5 min OK 0; 0; 0 0,0 23 6 23 5 min OK 0; 0; 0 0,0 2024 uc 23 2 23 5 min OK 0; 0; 0 0,0 23 4 23 5 min OK 1; 0; 0 0,3 23 6 23 5 min OK 0; 0; 0 0,0 * white pit : start of visible appearance of white corrosion products XPS Cr spectra Surtec 650 + PACS 297,5 ev Cr(VI) or Cr(III)? Socomore PACS post treatment is leading to a significant performance improvement in SST Generation of potential CrVI species in the coating (location?) and CrVI in the bath / rinsing tank needs to be assessed, in relation to ESH and REACH compliance

Summary chromate free pre-treatment of aluminium alloys Chromate containing processes / product CrVI process replaced Close to qualification TSA Anodising PSA Anodising Painted / Paint Primer Sealing, unpainted Bonding Primer Degreasing Alkaline Treatments Acidic Treatments Chemical Conversion Coating PT Painted / Paint Primer Unpainted Replacements for Chromic Sulphuric Acid based pickling processes are qualified and introduced In relation to requirements CAA anodising process is replaced by TSA or PSA Chromate free treatment solutions are available as CrVI CCC replacement Replacements of chromate based paint products are still a hard challenge to meet the technical requirements Wash Primer Other processes Painted / Paint Primer DPI Welding: LBW, FSW Chemical milling

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