| HS Code | 308913 |
| Chemical Type | Organic fluorescent dye |
| Physical Form | Solid crystalline powder |
| Appearance | Colored powder with fluorescent character |
| Purity Grade | Electronic/EL grade, high purity |
| Solubility | Soluble in organic solvents such as toluene, chloroform, and acetone |
| Water Solubility | Practically insoluble in water |
| Fluorescence Emission | Strong emission in the visible spectrum |
| Quantum Yield | High fluorescence efficiency |
| Thermal Stability | Stable at typical electroluminescent device processing temperatures |
| Photostability | Good resistance to light-induced degradation |
| Moisture Sensitivity | Low when stored under dry conditions |
| Storage Conditions | Keep sealed in a cool, dry, dark place |
| Primary Application | Dopant or emissive dye for electronic and electroluminescent devices |
As an accredited Special Dye BASF Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Special Dye BASF Electronic/EL Grade is supplied in sealed, light-resistant containers, ensuring purity and stability. Quantity: 1 kg per container. |
| Container Loading (20′ FCL) | 20′ FCL: palletized, sealed containers, protected from moisture and contamination, ensuring safe transport of BASF Electronic/EL Grade dye. |
| Shipping | Ship in clean, tightly sealed original containers, kept upright, dry, and protected from light, heat, and contamination. It is not classified as dangerous goods under ADR, IATA, or IMDG regulations. Ensure proper product labeling, accurate shipping documentation, and avoid transport alongside foodstuffs. |
| Storage | Store Special Dye BASF Electronic/EL Grade in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep protected from moisture and UV light. Avoid contact with strong oxidizers. Ensure container remains closed when not in use to preserve purity and performance. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored sealed, dry, and protected from light at recommended temperatures. |
A Special Dye BASF Electronic/EL Grade with phthalocyanine-core molecular architecture is incorporated directly into negative-tone acrylic-epoxy hybrid color filter photoresist formulations for thin-film transistor liquid crystal display (TFT-LCD) and organic light-emitting diode (OLED) on-cell color filter fabrication. The dye exhibits solubility in propylene glycol monomethyl ether acetate (PGMEA) solvent at ≥15 wt% solid loading at 25 °C, enabling direct dissolver addition during resist compounding without a separate bead-milling dispersion step. Industry compliance during color filter manufacturing is governed by IEC 62321-3-1:2013 for specific migration screening of hexavalent chromium, lead, cadmium, and mercury in display component substrates, REACH Regulation (EC) No 1907/2006 Annex XVII entries 50–59 for azo dye–derived aromatic amine restriction applicable to dye degradation products during thermal post-cure, and particulate cleanliness limits defined in ISO 14644-1:2015 Class 5 and Class 6 for photoresist coating bays. Formulation addition ratio is 0.7–2.5 wt% relative to total resist solids excluding solvent; at the upper bound, chromaticity coordinates saturate while optical density at 365 nm increases to 1.2–1.5/μm, which reduces exposure latitude by 15–20% on high-resolution mask aligners. Downstream production process: the dye is pre-dispersed in PGMEA at 20 wt% concentrate using a Cowles dissolver at peripheral speed 8–12 m/s for 20–30 min; the concentrate is blended with acrylate monomer, epoxy resin, hexamethoxymethylmelamine crosslinker, and photoinitiator in a planetary mixer under 200 Pa vacuum for 30–45 min to eliminate micro-bubbles; the resist is filtered through 0.2 μm polytetrafluoroethylene cartridge filters and spin-coated on 100 mm × 100 mm Corning Eagle XG alkali-free glass substrates at 1,200–1,800 rpm with 45–60 s spin dwell; pre-bake on a high-uniformity hotplate at 90–110 °C for 90–120 s removes residual solvent to <2% by thermal gravimetric analysis; vacuum contact exposure at 365 nm wavelength with dose 80–120 mJ/cm² through a chromium-on-quartz photomask; aqueous development in 0.04–0.06 wt% tetramethylammonium hydroxide (TMAH) at 23 ± 1 °C for 60–90 s; post-bake in a convection oven at 230 °C for 30 min to complete epoxy ring-opening crosslinking; the resulting color filter pixel has final film thickness 1.8–2.2 μm measured by contact profilometry per ISO 4518. Dye thermal decomposition onset measured by thermogravimetric analysis at 10 °C/min ramp rate in nitrogen atmosphere is 310–325 °C; cumulative post-bake thermal budget above 240 °C exceeding 60 min produces chromaticity drift greater than 0.005 in CIE 1931 coordinates. Terminal product types: 55-inch ultra-high-definition TFT-LCD television panels, on-cell polarizer-free OLED smartphone color filters, automotive center-stack display filters with specified operating temperature range −40 °C to +105 °C, and avionics cockpit display filters requiring sunlight readability under 100,000 lx ambient illumination.
| Addition ratio (wt% relative to solids) | Post-bake film thickness (μm) | CIE 1931 x-coordinate (red sub-pixel) | CIE 1931 y-coordinate (red sub-pixel) | Transmittance at 550 nm (%) | Contrast ratio (opaque/clear) |
|---|---|---|---|---|---|
| 0.7 | 1.80 | 0.638 | 0.334 | 82 | 1850 |
| 1.2 | 1.95 | 0.641 | 0.331 | 76 | 2400 |
| 1.8 | 2.05 | 0.644 | 0.328 | 69 | 3100 |
| 2.5 | 2.18 | 0.646 | 0.327 | 61 | 3700 |
The Special Dye BASF Electronic/EL Grade functions as a spectral down-conversion material interposed between an indium tin oxide (ITO)-coated polyethylene terephthalate (PET) transparent electrode and a barium titanate dielectric layer in alternating-current powder electroluminescent lamps. The dye is dispersed into a cyanoethyl pullulan (CEP) polymer binder selected for its high dielectric constant (15–20 at 1 kHz), at formulation addition ratio of 0.1–0.8 wt% relative to dry binder mass. Exceeding 1.2 wt% triggers concentration quenching: the emission luminance measured at 400 Hz and 115 V RMS declines by more than 35% relative to the optimum because intermolecular energy transfer to non-emissive aggregate states dominates singlet exciton relaxation. Conversely, below 0.05 wt% the spectral conversion efficiency is insufficient to correct the base ZnS:Cu phosphor emission from blue-green to the desired white chromaticity point. Compliance for AC powder EL lamp manufacturing: IEC 62368-1:2023 clause 5.3.1 for insulation coordination and electric strength testing, UL 393:2019 for electroluminescent luminaire and backlight safety, IEC 60065 legacy clause 9.1.1 for surge isolation from AC mains, and Directive 2011/65/EU (RoHS recast) as amended by (EU) 2015/863 for restricted substance ceilings including di(2-ethylhexyl) phthalate (DEHP) at <0.1 wt% in homogeneous materials. Downstream production process: screen printing of the dye-bearing conversion layer using stainless steel mesh with thread count 230–305 threads/inch, mesh tension 20–25 N/cm, and capillary film emulsion thickness 20–30 μm; wet laydown controlled to 35–45 μm by squeegee durometer 65–75 Shore A, blade angle 60–75°, and print speed 40–80 mm/s; drying in an infrared convection tunnel at 120–135 °C for 3–5 min until residual solvent is below 2 wt%; a subsequent dielectric layer of barium titanate powder dispersed in the same CEP binder is printed at 20–25 μm wet thickness and dried; a rear electrode of silver flake paste is printed and cured at 120 °C for 10 min; final lamination of the PET/ITO front electrode to the printed stack uses a roll laminator at nip pressure 0.3–0.5 MPa and roll temperature 60–80 °C. Pre-drying of the dye powder at 80 °C for 4 h is mandatory when ambient relative humidity exceeds 60%, because adsorbed moisture hydrolyzes cyanoethyl pullulan during drying and forms microlens defects. Direct contact with amine-cured epoxy encapsulants is contraindicated: amine groups protonate the dye chromophore, shifting emission maximum by 18–25 nm toward shorter wavelength and reducing photoluminescence quantum yield by 40–55%. Terminal product types: electroluminescent backlights for automotive instrument cluster needles and dials, wearable safety illumination strips on industrial high-visibility garments, aircraft cabin floor-path emergency egress lighting systems, keypad backlights for explosion-proof industrial terminals, and retail point-of-sale edge-lit panel graphics.
| Standard designation | Clause/method | Scope of requirement | Test condition |
|---|---|---|---|
| IEC 62368-1:2023 | 5.3.1 | Electric strength insulation | 27.6 kV DC minimum withstand |
| UL 393:2019 | 13 | Flame rating of polymeric materials | Horizontal burn test, 12 mm/min maximum |
| IEC 60065 | 9.1.1 | Surge isolation from AC mains | 1.5 kV impulse, 3 s |
| RoHS (EU) 2015/863 | Full material | DEHP, DIBP, BBP, DBP individual ceilings | <0.1 wt% homogeneous material |
| ASTM D1003-21 | Haze measurement | Optical clarity of ITO/PET front electrode post-lamination | Haze <5% at 550 nm |
Fabrication of dye-sensitized solar cells using the Special Dye BASF Electronic/EL Grade as a panchromatic metal-free organic sensitizer requires sequential execution of three production stages: mesoporous titanium dioxide photoanode deposition, dye chemisorption from solution, and I₃⁻/I⁻ redox electrolyte encapsulation with a platinized counter electrode. The dye solution is prepared by dissolving the product in anhydrous acetonitrile and tert-butanol at 1:1 v/v ratio, with dye concentration maintained at 0.2–0.5 mM; chenodeoxycholic acid is added as co-adsorbent at 1:10 molar ratio relative to dye to suppress TiO₂ surface electron recombination. Photoanode substrate preparation: fluorine-doped tin oxide (FTO) glass with 7 Ω/sq sheet resistance is cleaned by ultrasonic agitation in acetone (15 min), isopropanol (15 min), and deionized water (10 min) at 37 kHz; a compact TiO₂ blocking layer is spray-deposited at 450 °C from titanium diisopropoxide bis(acetylacetonate) precursor; the mesoporous layer is screen-printed or slot-die coated using an anatase nanoparticle paste with mean particle size 20–25 nm, controlled wet thickness 12–18 μm, baked at 125 °C for 10 min, then sintered in a box furnace with temperature ramp 5 °C/min to 500 °C for 30 min; after cooling to 80 °C, the electrode is immersed in the dye solution for 16–24 h in the dark at 25 °C under nitrogen atmosphere to prevent dye oxidation. Electrolyte filling and sealing: the counter electrode is a 3–5 nm platinum film deposited by thermal evaporation on FTO glass; the two electrodes are sealed using a 25 μm Surlyn ionomer gasket laminated at 110–120 °C for 60 s; the I₃⁻/I⁻ electrolyte comprised of 0.6 M 1-butyl-3-methylimidazolium iodide, 0.03 M iodine, and 0.1 M guanidinium thiocyanate in acetonitrile is back-filled through predrilled fill ports under 10⁻² mbar vacuum, and ports are sealed with Surlyn and cover glass. Compliance: IEC 60904-1:2020 defines I–V curve measurement procedure with four-wire Kelvin connections; IEC 60904-3:2019 references ISO 9845-1:2022 for the standard AM1.5G reference solar spectral irradiance distribution; IEC 60904-8:2014 provides spectral responsivity measurement for external quantum efficiency; and IEC 61646 legacy clauses remain relevant in procurement specifications for thin-film terrestrial photovoltaic module durability. Production-scale batch failure mode observed on slot-die coating equipment: edge-thickening at substrate margins produces local dye loading variation exceeding ±15% of target areal density, which manifests as visible chromatic non-uniformity in the finished cell and requires intermittent ultrasonic bath agitation at 37 kHz during dye adsorption to maintain uniform chemisorption kinetics. Terminal product types: indoor photovoltaic cells for wireless sensor network nodes delivering 15–35 μW/cm² power density at 200–1,000 lx white LED illumination, building-integrated semitransparent photovoltaic façade glass with visible light transmittance 30–45% and nominal power conversion efficiency 4–6% under AM1.5G, self-powered environmental monitoring tags for logistics cold-chain tracking, and solar-powered electronic shelf labels for retail display.
In semiconductor lithography at 365 nm (i-line) exposure wavelength, the Special Dye BASF Electronic/EL Grade is formulated into a sacrificial contrast enhancement layer (CEL) that is spin-coated as a topcoat above conventional positive-tone diazonaphthoquinone/novolac photoresist to attenuate out-of-focus reflected radiation from high-topography substrates such as polysilicon gate stacks and shallow trench isolation fields. The dye loading in a water-soluble poly(vinyl alcohol) or poly(acrylic acid) CEL matrix is 1.5–3.0 wt% relative to polymer solid; absorbance at 365 nm is tuned to optical density 0.8–1.5/μm, which corresponds to transmittance reduction to 35–55% per micron of CEL thickness. The result is measured contrast improvement of 20–40% relative to undyed photoresist at identical substrate reflectivity, as quantified by residual resist thickness after development per SEMI P6-0301. Compliance in wafer fabrication: SEMI S2-0823 for semiconductor equipment safety evaluation, SEMI S8-0723 for ergonomics engineering of wafer handling stations, ISO 14644-1:2015 Class 3 cleanroom particle limits for lithography processing bays, and SEMI P3-92 for photoresist material specification format. Downstream production process: hexamethyldisilazane (HMDS) vapor priming at 120 °C for 60 s to promote resist adhesion; photoresist spin coating at 2,500–3,500 rpm for 30–45 s to achieve film thickness 1.0–1.3 μm; softbake at 90–110 °C for 60 s on a proximity hotplate; CEL spin coating at 1,500–2,000 rpm from an aqueous solution to thickness 0.4–0.6 μm; exposure using an i-line stepper with numerical aperture 0.48–0.62, partial coherence 0.6–0.7, and exposure dose 120–180 mJ/cm² compensated for CEL absorption; removal of the CEL topcoat by deionized water rinse at 23 °C for 30–45 s; development in 2.38 wt% tetramethylammonium hydroxide developer for 60–90 s with puddle or spray dispensing. Critical process constraint: the CEL topcoat must be applied within 2 h of resist softbake completion; exceeding this interval causes interfacial dewetting because residual solvent in the resist film diffuses to the surface and lowers CEL solution surface tension below 30 mN/m, producing pinhole defects. Published data for this specific dye configuration in high-volume production is limited, and process qualification requires wafer-level statistical validation per SEMI C30-1118. Terminal product types: CMOS image sensor wafers with 1.1 μm pixel pitch, power MOSFET devices with gate trench depth 0.8–1.2 μm, MEMS accelerometer proof-mass structures requiring 3–5 μm feature depth, and automotive microcontroller wafers with 0.18–0.35 μm design rule nodes.
The Special Dye BASF Electronic/EL Grade is compounded into a biphenyl epoxy-phenol novolac hardening system epoxy molding compound (EMC) for semiconductor package laser marking, in which focused 1064 nm near-infrared irradiation induces localized dye thermo-oxidative carbonization producing dark, high-contrast alphanumeric characters on the package surface. The formulation addition ratio operates within a narrow threshold window of 0.05–0.3 wt% relative to total EMC mass. Below 0.05 wt%, the contrast ratio between marked and unmarked package surface falls below 2:1 as measured on ICC profile grayscale calibration with a calibrated optical densitometer per ISO 5-3:2009, rendering the marking illegible to automated vision inspection systems. Above 0.3 wt%, the EMC spiral flow length measured per SEMI G61-0321 decreases by more than 10% relative to the unloaded formulation because dye particles increase filler-filler interaction and reduce resin melt flow under transfer molding conditions; this degradation can lead to incomplete cavity filling in fine-pitch QFN packages with 0.4 mm minimum pad-to-pad clearance. Compliance: IPC/JEDEC J-STD-020F for moisture/reflow sensitivity classification of plastic integrated circuit surface-mount devices, IEC 60749-26 for semiconductor device package solderability test method (dip-and-look test at 235 °C ± 5 °C for 2 s), Directive 2011/65/EU (RoHS) lead and cadmium restriction ceilings of 0.1 wt% and 0.01 wt% respectively in homogeneous material, and IEC 61249-2-21 for halogen-free printed circuit board laminate baseline material compatibility. Downstream production process: twin-screw extrusion compounding using a co-rotating twin-screw extruder with screw L/D ratio 32:1 to 44:1, barrel temperature profile 75–110 °C across 9–12 zones, screw speed 200–350 rpm, throughput 15–30 kg/h; the dye is pre-mixed into fused silica filler at 1:100 masterbatch ratio using a high-speed mixer operating at 1,500–2,500 rpm for 10–15 min to ensure spatial homogeneity before compounding; the extruded EMC sheet is ground to 100–200 μm particle size and pressed into cylindrical preforms; transfer molding is conducted at mold temperature 175 °C with transfer pressure 6.9–9.8 MPa and cure time 70–120 s; post-mold cure in a nitrogen convection oven at 175 °C for 4–6 h completes crosslinking; laser marking is performed using a Q-switched 1064 nm Nd:YAG laser with pulse repetition frequency 1–10 kHz, spot diameter 40–80 μm, and scan speed 200–600 mm/s. Incompatibility constraint: the dye must not be pre-blended with amine-functional silane coupling agents during silica filler surface treatment, because premature nucleophilic ring-opening reaction shifts the dye absorption maximum from 1064 nm to 980–1020 nm, reducing laser energy absorption efficiency by 30–50% and causing incomplete marking character formation. Terminal product types: QFN (quad-flat no-leads) packages with body size 3 mm × 3 mm to 10 mm × 10 mm, SOIC leadframe devices with 1.27 mm lead pitch, insulated-gate bipolar transistor (IGBT) power module housings with operation temperature up to 150 °C junction temperature, and smart card microcontroller module encapsulations with total package thickness 580–650 μm.
Solution-processed bulk heterojunction organic photodetectors (OPDs) incorporating the Special Dye BASF Electronic/EL Grade as a photosensitizer require precise control of blend morphology in a poly(3-hexylthiophene-2,5-diyl):[6,6]-phenyl-C₆₁-butyric acid methyl ester (P3HT:PCBM) active layer at addition ratio 0.5–5.0 wt% relative to total photoactive material mass. The dye's high molar extinction coefficient (1.2–2.8 × 10⁴ M⁻¹cm⁻¹) in the 550–650 nm spectral window extends the photodiode's external quantum efficiency response to match photopic ambient light conditions with incandescent or white LED light sources. Compliance: IEC 62471:2006 for photobiological safety of lamps and lamp systems applicable when the OPD is integrated into a photoplethysmography illumination module, ISO 13485:2016 for medical device quality management systems where the OPD functions as the sensing element in a pulse oximetry front end, and IEC 62368-1:2023 for safe integration into information technology equipment. Downstream production process: the indium tin oxide (ITO)-coated glass or polyethylene naphthalate substrate is cleaned in an oxygen plasma chamber at 100 W radio-frequency power for 5 min; a poly(3,4-ethylenedioxythiophene):polystyrene sulfonate (PEDOT:PSS) hole transport layer is spin-coated at 3,000 rpm for 30 s to thickness 40–60 nm, followed by annealing at 120 °C for 10 min; the P3HT:PCBM:dye blend solution in anhydrous chlorobenzene or 1,2-dichlorobenzene is blade-coated with coating gap 100–150 μm and substrate speed 10–25 mm/s, yielding a photoactive film thickness of 80–120 nm after solvent evaporation; thermal annealing on a calibrated hotplate at 120–140 °C for 10–20 min in a nitrogen-atmosphere glovebox (O₂ <1 ppm, H₂O <1 ppm) promotes P3HT crystallization and PCBM phase segregation; the aluminum cathode is deposited by thermal evaporation at 1 × 10⁻⁶ mbar base pressure to thickness 100 nm through a shadow mask defining 2–4 mm² active area. Operational boundary: device external quantum efficiency degrades by 15–25% after 500 h continuous illumination at 100 mW/cm² (1 sun equivalent) when encapsulation moisture permeability exceeds 1 × 10⁻⁴ g/m²/day; glass-to-glass encapsulation with UV-curable epoxy edge sealant and integrated desiccant getter is therefore required for service lifetimes exceeding 5,000 h. Terminal product types: flexible organic photodetector arrays for reflectance-mode pulse oximetry sensors, industrial incremental optical encoders requiring 1 μs photoresponse time, ambient light sensors for smartphone display brightness control with dynamic range 10⁻³–10⁵ lx, and printed organic image sensors for document scanning applications.
The Special Dye BASF Electronic/EL Grade is formulated into covert authentication ink systems for electronic component traceability and anti-counterfeiting applications, leveraging narrow-band near-infrared fluorescence emission at 680–720 nm under 640 nm laser excitation to enable machine-readable verification isolated from ambient visible illumination. Addition ratio in the final ink vehicle is 0.01–0.1 wt% relative to total ink mass; at 0.1 wt%, printed fluorescence intensity measured by a calibrated scanning fluorimeter (excitation 640 nm, emission integration 660–740 nm) reaches 1 × 10³ cps against substrate background noise of ≤50 cps, yielding signal-to-noise ratio ≥20:1. Compliance: ISO 14298:2013 for management of security printing processes, including clause 4.2 on documented security risk assessment and clause 7.3 on secure storage of authentication materials; ISO 18385:2016 for minimizing the risk of human DNA contamination in products used to collect, store, and analyze biological material for forensic purposes, relevant when authentication labels enter forensic evidence chains; REACH Annex XVII entry 43 for azocolourants restrictions applicable to dye breakdown products when labels are thermally destructed; and DIN 16514:2018 for printing ink terminology and classification (B3 fluorescent ink category). Downstream production process: nano-milling of the dye suspension in a horizontal bead mill using 0.3 mm zirconia ceramic grinding media at bead fill ratio 80–85%, chamber cooling to maintain ≤30 °C slurry temperature, circulation grinding time 45–90 min, with final particle size verified by photon correlation spectroscopy to D₉₀ <200 nm and polydispersity index <0.15; the milled dye dispersion is blended with a phenoxy resin/ethyl cellulose ink vehicle at 2,000 rpm for 15–20 min and filtered through 1.0 μm absolute-rated polypropylene depth filters; printing is performed on roll-to-roll inkjet equipment using piezoelectric printheads with nozzle diameter 35–80 μm, drop volume 3–12 pL, firing frequency 8–20 kHz, and web speed 15–50 m/min; inline drying for water-based formulations uses infrared panels at 60–90 °C surface temperature, while UV-LED curing at 395 nm wavelength with dose 250–500 mJ/cm² is used for UV-curable inkjet formulations. Chemical incompatibility constraint: the fluorescent dye must be stored separately from acid-functional acrylic ink resins with acid value >15 mg KOH/g because esterification at storage temperatures above 40 °C reduces emission quantum yield by more than 50% over a 6-month shelf-life window. Terminal product types: anti-tamper authentication labels for application-specific integrated circuit (ASIC) chips and field-programmable gate array (FPGA) devices, holographic security decals for server module chassis with tamper-evident frangible adhesive, forensic taggant varnishes for lithium-ion battery packs requiring supply chain traceability, and covert machine-readable markings on printed circuit board edge connectors.
Doping of polymethyl methacrylate (PMMA) step-index polymer optical fiber cores with the Special Dye BASF Electronic/EL Grade enables wavelength-selective absorption tuning for short-haul datacom and display illumination applications where spectral shaping of transmitted light is required. The dye is introduced during bulk radical polymerization of methyl methacrylate monomer at addition ratio 0.05–0.5 wt% relative to monomer mass, initiated by azobisisobutyronitrile (AIBN) at 0.1–0.2 wt% relative to monomer. The preform polymerization is conducted in a sealed borosilicate glass tube reactor with inner diameter 10–16 mm, placed in a water bath at 50–60 °C for 48–72 h, followed by post-cure temperature ramp to 90–110 °C for 12 h to reduce residual monomer content below 0.5 wt%. The doped PMMA core preform is subsequently drawn into optical fiber on a vertical draw tower with zone-controlled infrared furnace temperature 210–230 °C across 3 heating zones, draw speed 0.5–2.0 m/s, and active outer diameter feedback control maintaining 1.0 mm nominal diameter within ±5 μm tolerance; a fluorinated polymer cladding is applied inline by co-extrusion or co-drawing. Compliance: IEC 60793-2-40:2021 for category A4a.2 step-index polymer optical fiber specifications including minimum bandwidth-distance product and attenuation limits; ISO 11801-1:2017 for generic cabling performance requirements in information technology networks, which references IEEE 802.3bv for gigabit Ethernet over plastic optical fiber; and IEC 61754-20 for mechanical interface standards of POF connectors (F07 type). The dye addition ratio above 0.5 wt% introduces excessive Rayleigh scattering from molecular aggregates that increases attenuation at 650 nm (the standard PMMA low-loss window) beyond 200 dB/km, which violates the IEC 60793-2-40 channel attenuation budget for 100 m point-to-point link distances. Terminal product types: industrial fieldbus POF cables for PROFINET and SERCOS III real-time automation networks requiring immunity to electromagnetic interference, automotive MOST (Media Oriented Systems Transport) optical ring networks for infotainment data distribution at 25–150 Mbit/s, side-glow fiber for ambient LED interior lighting with uniform luminance along 5–10 m lengths, and sensor-grade POF for optical level sensing in fuel storage tanks where intrinsic safety requirements preclude metallic conductors.
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Electroluminescent device fabrication imposes a narrower ion-contamination window than conventional polymer coloration. Special Dye BASF Electronic/EL Grade is supplied as an undiluted organic colourant for evaluation in emission-layer, colour-conversion, and optoelectronic host–guest systems. The product identity is controlled by batch certificate rather than a single numerical model; regional BASF material numbers may differ. The powder is free-flowing and is screened through a 100 µm sieve with a residue target of ≤0.1 % w/w per ISO 787-18:1983. The grade is soluble at processing concentrations in methyl ethyl ketone, ethyl acetate, and toluene. Chlorinated aromatic solvents such as chlorobenzene require pre-testing for reducible chlorine impurities because of the product’s sensitivity to residual chlorinated species in emissive layers. The product is not intended for direct food-contact or medical-implant layers without additional purity verification.
Electronic-grade differentiation is achieved through post-synthesis purification rather than through the addition of binder resins or carrier waxes. The specification framework includes assay, water content, matter volatile at 105 °C, non-volatile residue, and trace-metal contamination. Published data for this specific BASF configuration is limited; the table below is a consolidated control window typical of electronic-grade soluble dye acceptance in display manufacturing, not a substitute for the lot certificate. Reversed-phase HPLC-UV is used for assay, with a C18 stationary phase and acetonitrile–water gradient; peak purity is checked at 254 nm and 430 nm where applicable. Trace-metal analysis after closed-vessel acid digestion should be performed with ICP-MS or ICP-OES to confirm that alkali and alkaline earth ions remain below the electroluminescent stability threshold.
| Parameter | Method/Detector | Electronic/EL Grade Control Window |
|---|---|---|
| Assay | HPLC-UV area percent | ≥98.0 area% |
| Water content | ISO 760:1978 | ≤0.50 % w/w |
| Matter volatile at 105 °C | ISO 787-2:1981 | ≤1.0 % w/w |
| Residue on 100 µm sieve | ISO 787-18:1983 | ≤0.1 % w/w |
| Trace sodium, potassium, calcium, iron, magnesium | ICP-MS per ISO 17294-2:2016 | each ≤10 mg/kg; total ≤50 mg/kg |
| Halogen content | EN 14582:2016 | ≤900 mg/kg total |
Technical-grade solvent dyes may contain sodium sulfate or chloride process salts that are acceptable in lacquers but interfere with electroluminescent stability. The electronic-grade material is washed or membrane-purified to move alkali and alkaline earth ions below the thresholds shown. Mobile cations in an emissive layer can accumulate at the indium tin oxide interface, shift injection voltage, and enlarge dark-spot defects during continued operation. Each incoming lot should be verified by ICP-MS or ICP-OES before use in a production emission stack.
In a production-scale sheet-fed screen-print line for electroluminescent pastes, the dye is dissolved first in a high-boiling ester or aprotic solvent, then let down into a polyester or polyurethane binder. High-shear dispersion equipment is used only for binder wetting; rotor tip speed below 8 m/s avoids gel nucleation in polyurethane systems. Slot-die coating of colour-conversion films requires filtration through a 0.45 µm absolute filter; screen-print pastes are typically filtered through a 1.0 µm filter, with the mesh opening controlling larger defects. Initial solvent removal at 80 °C for 10 min followed by thermal crosslinking at 120 °C to 130 °C for 15 min to 20 min is used for polyester-melamine binders. For continuous roll-to-roll coating, a two-zone dryer with first-zone temperature 70 °C and second-zone temperature 110 °C reduces solvent skin-over. At relative humidity above 60 %, powder pre-drying at 60 °C under vacuum for 4 h is required to prevent micro-condensation haze in the dried layer.
Drying and cure schedules are not merely cosmetic; they control dye migration. At dry-film thicknesses below 10 µm, a fast solvent flash can supersaturate the binder and cause dye recrystallisation at the surface, producing filterable defects. On a production line, a two-stage profile with a slower first-stage ramp is therefore preferable to a single high-temperature zone. In polyester-based electroluminescent pastes, the first stage removes free solvent while the binder remains partially open; the second stage completes crosslinking and locks the dye into the polymer matrix. If the first stage is skipped or shortened below 5 min, retained solvent in the bulk film can form pinholes during the crosslinking step and increase the probability of dielectric breakdown.
Differences from other products become material when the dye operates in an electric field. Conventional solvent dyes for lacquers and printing inks can retain sodium, potassium, and sulfate process residues at concentrations sufficient to increase ionic conductivity in a polymer layer. The electronic-grade specification reduces these residues by salt-free washing or membrane purification, which maintains chromaticity while limiting mobile-ion migration to the ITO interface. It also avoids free aromatic amine additives and carrier resins that would volatilize under high-vacuum deposition or generate non-emissive recombination centres. The limitation is likewise defined: this grade is not compatible with amine-based adhesion promoters in polyurethane binders, because base-catalysed dye–binder reactions can produce insoluble complexes and a measurable chromaticity shift. If a formulation requires an aminosilane adhesion layer, the dye should be isolated from that layer by an intervening dielectric or barrier film.
Compared with pigment dispersions of similar hue, the soluble electronic-grade dye does not contribute particulate scattering. A pigment dispersion with median particle diameter near 200 nm can reduce transmitted colour intensity through scattering, whereas the molecularly dissolved dye remains below scattering thresholds at normal use concentrations. The trade-off is migration resistance: a dissolved dye can diffuse during high-temperature cure, so the drying and crosslinking schedule must be designed to restrict mobility. If migration fastness is the primary requirement and optical scattering is tolerable, a pigment dispersion may be appropriate. If the application is an emission layer or a colour-conversion film where optical clarity and low haze are required, the electronic-grade soluble dye is preferred only after the solubility limit in the selected binder system is confirmed by phase-separation testing over 72 h at 25 °C and at the planned cure temperature.
Vacuum thermal evaporation is a further process where grade purity separates this product from standard colourants. Technical-grade dye batches may contain non-volatile inorganic salts that remain in the crucible and reduce sublimation yield. Electronic-grade material reduces these non-volatile residues, but evaporation behaviour is not quantified by a single specification value. Deposition engineers should request lot-specific residue-on-ignition data and evaluate sublimation onset by thermogravimetric analysis under reduced pressure. A dedicated quartz crucible with source temperature control within ±2 °C is recommended to avoid decomposition bands near the deposition window. The product should not be sublimed from stainless steel boats that contain residual chromium or nickel oxide scale, because these surfaces can catalyse chromophore decomposition.
Analytical failure modes on manufacturing lines most commonly involve either insufficient drying or unintended solvent exchange. If the powder is stored in a partially opened container at RH >60 %, surface moisture can promote agglomeration and produce screen clogging. If the dye is transferred into a solvent blend containing high-boiling ketones without confirming solubility, a portion may remain as suspended crystallites that pass dispersion filtration and later deposit as dark specks. For this reason, incoming raw-material evaluation should include a solution clarity test in the selected production solvent after 24 h equilibration at 25 °C and after cold storage at 5 °C for 72 h. A visible haze or filterable residue at the lower temperature indicates a solubility margin that may be inadequate for roll-to-roll coating.
Electronic/EL Grade is placed on the market with documentation generated under chemical-management and quality-system requirements. The product is not currently specified as food-contact grade; applications requiring direct food contact or pharmaceutical use should be validated under separate protocols. Compliance claims are tied to the specific lot certificate and the analytical methods listed in the certificate of analysis. Absence of a listed substance in the certificate should not be interpreted as a universal negative unless the method limit is recorded.
| Obligation | Reference Standard/Clause | Boundary Applied to This Grade |
|---|---|---|
| REACH safety data sheet | Regulation (EC) No 1907/2006, Annex II | SDS in official language of receiving market; lot-specific certificate of analysis available |
| RoHS restricted substances | Directive 2011/65/EU Annex II; IEC 62321-5:2013, IEC 62321-6:2015, IEC 62321-7-1:2015 | Below maximum concentration values in homogeneous material by weight |
| Halogen-free electronic assembly | IEC 61249-2-21:2003 | Bromine ≤900 mg/kg; chlorine ≤900 mg/kg; total ≤1500 mg/kg |
| Quality management | ISO 9001:2015 | Batch traceability from dye intermediate synthesis through packaging |
Storage should keep containers sealed at ≤30 °C and relative humidity below 50 %. The product should not be combined with strong oxidizers, peroxides, or nitrating agents; contamination with these materials may alter the dye chromophore and generate non-emissive side products. In solvent-based electroluminescent ink production, pre-drying of the dye is recommended before exposure to moisture-sensitive polyurethane intermediates. Retained samples from each lot should be held under inert gas and protected from ultraviolet light for the duration of the production campaign. Lot-to-lot variation in trace-metal content, water content, and sieve residue should be trended using control charts against the methods already listed; a sudden increase in sodium or potassium above 10 mg/kg may indicate a purification excursion and warrants quarantine before the material is released into an active emission-layer coating line.