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Alumina Polishing Slurry Electronic/EL Grade

    • Product Name: Alumina Polishing Slurry Electronic/EL Grade
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 343553
    Product Alumina Polishing Slurry Electronic/EL Grade
    Chemical Composition Alpha-alumina (α-Al2O3) in deionized water
    Appearance White milky liquid suspension
    Particle Size D50 0.05-1.0 µm depending on grade
    Solid Content 10-50 wt% depending on grade
    Purity ≥ 99.99% (4N)
    Ph 3-11 depending on formulation
    Density 1.1-1.6 g/cm³ at 25°C
    Viscosity 10-500 mPa·s at 25°C
    Dispersion Medium Ultrapure deionized water
    Particle Morphology Spherical or polyhedral crystalline
    Zeta Potential ±20 to ±50 mV depending on pH
    Shelf Life 6 to 12 months sealed

    As an accredited Alumina Polishing Slurry Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 5 kg sealed HDPE containers, this Electronic/EL Grade alumina polishing slurry ensures controlled particle size and high purity.
    Container Loading (20′ FCL) 20′ FCL loading of Electronic/EL Grade alumina polishing slurry; use sealed, clean container, secure drums/pails, prevent leakage, avoid contamination.
    Shipping Alumina Polishing Slurry (Electronic/EL Grade) ships in sealed HDPE drums or IBC totes, kept upright to prevent leakage. Typically non-hazardous/non-DG, but protect from freezing, contamination, and extreme heat. Include product labels, SDS, COA, and handling documentation to ensure safe, clean transport.
    Storage Store alumina polishing slurry (Electronic/EL Grade) in tightly sealed, clean containers to prevent contamination. Keep in a cool, dry, well-ventilated area away from direct sunlight, extreme heat, or freezing temperatures. Avoid exposure to dust or moisture. Stir gently before use to ensure uniformity, and follow manufacturer’s shelf-life guidelines for optimal performance.
    Shelf Life Shelf life is typically 6-12 months if stored sealed at room temperature, protected from freezing and contamination.
    Application of Alumina Polishing Slurry Electronic/EL Grade

    On c-plane sapphire LED wafer manufacturing lines, the transition from 2-inch to 4-inch and 6-inch wafer formats has forced polishing slurry vendors to control particle aggregation across longer residence times in recirculating distribution loops. Electronic/EL-grade alumina polishing slurry is specified after diamond lapping, where subsurface damage depth can extend to 200–500 nm beneath the mechanically stressed surface. The polishing process uses single-sided or double-sided planetary polishers with polyurethane pads, platen speeds of 20–60 rpm, applied downforce of 3.4–10.3 kPa, and slurry flow rates scaled to 50–200 mL/min per 150 mm wafer equivalent. The abrasive phase typically comprises high-purity alpha-alumina particles with a median particle size of 80–150 nm and a solids loading of 20–30 wt%; suspension is maintained by electrostatic stabilization, with zeta potential values exceeding ±30 mV depending on pH. At pH 10–11, alumina solubility at the sapphire surface is sufficient to create a hydrated aluminum oxide reaction layer that is removed by mechanical action, while the bulk sapphire remains crystalline. Removing the hydrated layer requires controlled downforce because excessive mechanical energy generates subsurface cracks rather than material removal. Production-scale defect audits show that large-particle counts greater than 0.5 µm must be held below 1000 counts/mL to protect LED epi-ready wafer yield; submicrometer filtration with 0.5 µm point-of-use filters is common. Post-polish surface roughness measured by atomic force microscopy according to ISO 25178-2:2021 is typically below 0.3 nm Ra for epi-ready sapphire, and wafer bow/total thickness variation is monitored by interferometry. In high-volume LED production, the same slurry batch may remain inside the distribution loop for 8–24 h, which makes batch-to-batch viscosity drift and aggregate formation critical process variables. Published data from CMP equipment manufacturers indicate c-plane sapphire removal rates between 1.5 and 3.5 μm/h under these conditions, but removal rate alone is not the acceptance criterion; defect density, surface roughness, and post-clean aluminum residue must all remain within the downstream MOCVD growth specification.

    How Does Alumina Slurry Manage Step Height on Basal Plane SiC?

    After diamond lapping exposes subsurface damage, alumina-based CMP is one of the abrasive options inserted before colloidal silica final buffing on monocrystalline silicon carbide wafers. The material mismatch between 9-Mohs hardness alumina and hexagonal SiC means that the slurry must operate in a narrow mechanical window: insufficient downforce leaves step-bunching and lapping tracks, while excessive downforce creates deep scratches that cannot be removed by the final silica buffer. Production rotary CMP tools for 150 mm and 200 mm SiC wafers frequently use hard polyurethane pads with in-situ diamond pad conditioners, platen linear velocities of 0.6–1.2 m/s, and downforce of 20–50 kPa. The slurry itself is typically adjusted to pH 8–10 with an oxidizer package that promotes the formation of a silicon oxide reaction film on the basal plane; manufacturer-specific oxidizer blends are proprietary. Friction coefficient and motor current are used to detect the removal of the damage layer because optical endpoint is confounded by wafer transparency. Post-polish atomic force microscopy according to ISO 25178-2:2021 is used to quantify step height and residual roughness; after final buffing, Ra values below 0.1 nm are reported in power device wafer inspection. The process conflict that dominates this segment is selective etching at threading dislocations extending through the wafer: if the slurry pH or oxidizer concentration drifts upward, dislocation-related pits become visible as localized dark spots after KOH defect etching at 480 °C. Published data for this specific configuration is limited because SiC substrate suppliers treat polishing chemistry and pad-conditioning protocols as proprietary, but the field observation is consistent: a bimodal alumina particle distribution may increase removal rate while simultaneously raising the density of shallow scratches.

    Tungsten via planarization on 300 mm logic wafers is not a pure mechanical polish; the alumina slurry carries an oxidizer package that converts the tungsten surface into a softer tungsten oxide film removed by the abrasive. The alumina abrasive in this application is usually smaller than sapphire-grade material, with a median particle size of 50–120 nm, and the slurry is maintained at pH 2–4 using a ferric nitrate or hydrogen peroxide oxidizer system. Solids loading is typically lower, in the 5–15 wt% range, because high solids content accelerates pad glazing and increases the frequency of post-CMP alumina residue defects. In production, the primary process conflict is dense-array oxide erosion and via plug dishing: a tungsten removal rate above 250 nm/min may be achieved while the TEOS oxide removal rate is held below 5 nm/min, but only if pad temperature and slurry pH are tightly regulated. The endpoint signal is derived from optical reflectance change as tungsten clears from the field region; however, over-polishing beyond 30–60 s after endpoint produces measurable via dishing of 20–50 nm on logic test structures. Multi-platen CMP tools offer a dedicated tungsten platen, but cross-contamination risk remains if the same wafer path is used for copper. Alumina-bearing acidic tungsten slurry must be segregated from copper CMP waste streams because aluminum and tungsten ions can destabilize the complexing agents used in copper removal chemistries. Post-CMP cleaning uses dilute ammonium hydroxide–hydrogen peroxide mixtures at 40–60 °C followed by brush scrubbing. The operational boundary is explicit: increasing oxidizer concentration beyond the supplier specification raises removal rate for a short period, then triggers pad glazing and tungsten pitting on the wafer edge.

    When Aluminum Nitride Substrate Roughness Must Drop Below 10 nm before Direct Bond Copper Lamination

    Direct bond copper lamination demands an aluminum nitride surface with low roughness, low waviness, and minimal hydrolysis damage because the substrate is subsequently exposed to high-temperature nitrogen and oxygen ambients. AlN thermal conductivity of 170–230 W/m·K makes it suitable for power module baseplates, but aqueous CMP introduces a chemical risk: aluminum nitride hydrolyzes at pH extremes, releasing ammonia and forming a soft aluminum hydroxide layer that increases measured roughness. For this reason, alumina slurry used on AlN is commonly pH-buffered near 6–7, and the wafer or substrate is not allowed to dwell in wet slurry for more than the polishing cycle time. After flat lapping on cast iron plates with diamond slurry, CMP is run on single-sided rotary polishers at platen speeds of 30–50 rpm and downforce of 10–20 kPa. The abrasive loading is generally 10–20 wt% with a median particle size of 100–200 nm. Production acceptance for thin-film metallization typically requires Ra below 10 nm measured by stylus profilometry according to ISO 21920-2:2021, and waviness below 1 µm TIR over a 50 mm scan length. The process control problem is not removal rate but surface chemical stability: if the pH drifts above 7, the near-surface AlN converts to aluminum oxyhydroxide, and post-CMP drying creates a cloudy residual film that cannot be cleaned by standard solvent rinses. Published data for alumina slurry on AlN in production power-module lines is limited, but the known incompatibility with aggressive alkaline cleaners is a fixed boundary condition for this downstream segment.

    Downstream process control matrix for electronic/EL-grade alumina polishing slurry
    Downstream substrateTypical pH windowSolids loadingAcceptance metric / standard
    c-plane sapphire LED wafer10–1120–30 wt%Ra 0.3 nm / ISO 25178-2:2021
    Basal plane silicon carbide wafer8–105–15 wt%Step height and Ra 0.1 nm after buff / ISO 25178-2:2021
    Aluminum nitride substrate6–710–20 wt%Ra 10 nm / ISO 21920-2:2021
    Zirconia ferrule end-face7–95–10 wt%Apex offset 50 µm / Telcordia GR-326-CORE

    Precision Glass and Fiber Connector Polishing Conditions

    Unlike borosilicate optical flats that may be polished with ceria, alumina slurry is specified for hard crown glass, fused silica, and ceramic ferrule end-face finishing where ceria removal rate is insufficient. In single-fiber connector manufacturing, the final end-face geometry for LC and SC connectors is controlled by Telcordia GR-326-CORE: radius of curvature between 7 mm and 25 mm, apex offset less than 50 µm, and fiber undercut within ±50 nm. Alumina slurry is applied either as a free-abrasive suspension or as a fixed-abrasive polishing film with particle size grades from 0.3 µm to 1.0 µm. Production polishing machines apply 0.5–2.0 N force per ferrule for 30–120 s during the final radius-forming step, with the slurry delivered in a low-flow mist or dropwise sequence to prevent slurry drying and particle agglomeration at the ferrule edge. The process window that must be preserved is fiber undercut bias: if the alumina abrasive removes the fiber end-face faster than the surrounding zirconia ferrule, undercut becomes negative and the fiber protrudes beyond the theoretical sphere. If the slurry is too aggressive on the zirconia body, the fiber appears recessed, producing a positive undercut that degrades return loss. Interferometric end-face geometry measurement is performed on 100% of connectors in high-reliability production lines. The refractive index mismatch between soft borosilicate glass and hard alumina is significant, so alumina slurry is not normally used as the final polish for fused silica fiber; it functions as the intermediate or ferrule-forming abrasive before cerium oxide final finishing.

    For 95 mm nickel-phosphorus plated aluminum substrates used in enterprise hard disk drives, the final CMP step must remove 1–3 µm of plated Ni-P while preserving sub-nanometer topography. The substrate enters CMP after electroless nickel plating, annealing, and diamond turning; alumina slurry is then used on double-sided polishing machines with planetary carriers, platen speeds of 20–40 rpm, and downforce of 5–15 kPa. Slurry flow rates of 100–300 mL/min per machine are typical, and the polishing pad is a closed-cell polyurethane with a hardness selected to avoid edge roll-off at the 95 mm outer diameter and 25 mm inner diameter. The slurry is acidic, generally pH 2–4, with an oxidizer such as hydrogen peroxide to convert the Ni-P surface into a removable nickel oxide film. Removal rates of 0.5–1.5 μm/h are reported on production double-side polishers, but the critical acceptance metric is not speed; it is the absence of nodule-induced scratches from plating defects. Post-CMP cleaning uses megasonic deionized water at 40–50 °C followed by vapor drying, because residual alumina particles on the Ni-P surface create read-write clearance variability. Surface roughness is measured by atomic force microscopy according to ISO 25178-2:2021, with Ra <0.3 nm and Wa <0.5 nm over a 1 mm scan length as common acceptance limits. The process boundary is narrow: if slurry pH falls below 2, the Ni-P surface roughens and pit defects increase; if pH rises above 4, removal rate collapses and the substrate retains diamond-turning marks that later impair fly-height control in the finished drive.

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    Certification & Compliance
    More Introduction

    Electronic-grade (EL) alumina polishing slurry is a high-purity aqueous dispersion of α-alumina (corundum, α-Al₂O₃) engineered for chemical–mechanical planarization (CMP) of sapphire, silicon carbide, gallium nitride, and selected metal interconnect layers in semiconductor, LED, and RF device manufacturing. The product class is defined by controlled trace-metal burdens below 10 ppm per element, median particle diameters (D50) between 200 nm and 500 nm, and deliberately narrow particle-size distributions with D90/D10 ratios below 3.0 as measured by ISO 13320:2020 laser diffraction. Model designations—typically rendered as EL-20, EL-50, or EL-100 prefixes—encode the nominal D50 in tens of nanometers or an application-specific surface-area target; exact naming conventions vary by supplier and are verified against the certificate of analysis. Production formulations operate at solids loadings of 20–30 wt%, exhibit zeta potentials exceeding |40 mV| at pH 9.8–10.5, and rely on anionic polymeric dispersants to prevent hard agglomerate formation during static storage and recirculating distribution. The slurry is supplied as a ready-to-use dispersion or as a 50 wt% concentrate requiring dilution with ultrapure water at point of use.

    Material Composition and Particle-Size Architecture

    The dispersed phase in EL-grade formulations is predominantly α-Al₂O₃, confirmed by X-ray diffraction; transition aluminas (γ-, θ-, and η-phases) are excluded because hydrated surfaces on these polymorphs promote viscosity instability and gelation in aqueous media. Trace-metal content—iron, sodium, potassium, and calcium—is controlled to below 5 ppm per element by ICP-MS methods aligned with SEMI C1, while total organic carbon is held below 50 ppb for front-end-of-line compatibility. Specific surface area, measured by ASTM D3663-20 (BET nitrogen adsorption), typically falls between 5 m²/g and 20 m²/g; primary crystallite morphology is verified by transmission electron microscopy as equiaxed or near-equiaxed rather than platelet- or acicular-type. Suspension pH is buffered at 9.8–10.5 for sapphire and SiC applications, while acidic variants with pH 3.5–4.5 are supplied for metal CMP where alkaline chemistry would corrode copper or tungsten features. Viscosity at 25 °C and 100 s⁻¹ shear rate, measured per ASTM D2196, is specified at 5–50 cP; the fluid exhibits mild pseudoplasticity with a power-law index of 0.85–0.95. Zeta potential is monitored by electrophoretic light scattering, and the lower stability threshold is |30 mV|; production lots falling below this value are rejected because the dispersant double layer can no longer overcome van der Waals attraction.

    Delivery to the platen is accomplished with peristaltic or low-pulsation diaphragm pump loops sized for 50–150 mL/min on 300 mm and 380 mm platens. Cavitating diaphragm pumps and high-velocity throttling valves are avoided because localized low-pressure zones induce microbubble collapse that promotes irreversible agglomeration. Point-of-use filtration through 0.5–1.0 μm depth-media cartridges removes incidental large agglomerates without stripping the dispersant; filter housing pressure differential is monitored and cartridge change is triggered at 103–138 kPa differential. Recirculation tanks are agitated with low-shear impellers at 30–60 rpm to inhibit sedimentation without degrading the particle-size distribution. Slurry temperature is maintained at 20–25 °C by jacketed vessels; excursions above 30 °C accelerate microbial metabolism in aqueous systems and shorten useful bath life, while excursions below 5 °C increase viscosity beyond the specified upper limit. On the tool, the slurry loop is configured with welded PVDF or polypropylene wetted surfaces; elastomeric seals of EPDM or Viton are selected because silicone rubber swells in contact with the dispersant package.

    How Does Electronic-Grade Alumina Differ from Colloidal Silica in Sapphire CMP?

    Silica-based slurries remove sapphire by a predominantly chemical route—silanol condensation across the Si–O–Al interface—supplemented by gentle abrasion from 20–80 nm soft particles of Mohs hardness 6.5–7. Alumina slurries operate primarily by mechanical abrasion, with 200–500 nm corundum particles of Mohs hardness 9 striking the substrate at controlled downforce. This hardness differential yields higher removal rates on c-plane sapphire at equivalent process parameters, but it also introduces a stronger dependence on particle-size tail control: any fraction above 1 μm becomes a direct scratch source. Residual contamination profiles diverge as well. Silica leaves a silicate-modified surface that complicates subsequent epitaxial nucleation; alumina residues are removed with dilute citric acid or megasonic DI water and do not contribute free silicon to the near-surface region. Defect-density targets for epi-ready sapphire require scratch densities below 1 mm⁻² and haze below 0.5 ppm on 50.8 mm and 100 mm wafers. Table 1 summarizes representative published ranges; production values vary with pad selection, downforce, and conditioner schedule.

    Representative comparative data for EL-grade alumina, colloidal silica, and standard optical alumina slurries on sapphire substrates.
    ParameterEL-Grade AluminaColloidal SilicaStandard Optical Alumina
    Purity≥99.99%≥99.9%≥99%
    D50200–500 nm20–80 nm1–5 μm
    Operating pH9.8–10.510.0–11.53.0–10.0 (unbuffered)
    Mohs hardness (dispersed phase)96.5–79
    Removal rate on c-plane sapphire2–6 μm/hr0.5–2 μm/hr5–15 μm/hr
    Post-polish Ra0.2–0.4 nm0.1–0.3 nm1–5 nm
    Principal process stageintermediate polishfinal polishrough lapping / pre-polish

    Concentrates at 50 wt% solids are shipped for dilution at point of use; dilution water must meet SEMI F57 ultrapure water specifications (resistivity 18 MΩ·cm at 25 °C, filtered through 0.1 μm membranes). Water is added to the concentrate under continuous agitation—never the reverse—to prevent localized dilution shock that collapses the electrical double layer. After dilution, the batch is stirred with a top-entry propeller at 100–200 rpm for 30 min and re-qualified by pH, viscosity, and D50 before release to the tool. In-line pH adjustment is performed with dilute KOH or HNO₃ metered at <0.5 mL/min; rapid acid or base addition above this rate generates localized precipitation zones that are not recoverable by stirring. Conductivity is recorded at the end of each adjustment step and cross-checked against the lot certificate of analysis.

    When Alumina Slurry Is Substituted for Diamond in Mid-Stage Polish

    Sapphire substrate processing commonly proceeds through three stock-removal stages: diamond rough lapping, alumina intermediate polish, and silica final polish. Introducing EL-grade alumina at the intermediate stage reduces subsurface damage depth from the 3–10 μm typical of free-abrasive diamond lapping to below 1 μm, as measured by cross-sectional transmission electron microscopy or molten KOH etch-pit density at 350 °C. The trade-off is removal rate: diamond slurry removes 10–30 μm/hr, while alumina formulations remove 2–6 μm/hr on c-plane sapphire at 27.6–41.4 kPa (4–6 psi) downforce and 50 rpm platen speed on a single-side polisher. Hard polyurethane pads with 55–65 Shore D hardness are specified; pad conditioning with an A160 diamond disc is performed every 10–15 min of polish time to prevent glazing. Edge exclusion is maintained below 3 mm on 100 mm wafers by optimizing the carrier film cut-out diameter. Published data for alternative pad geometries or double-side tool configurations is limited.

    Sealed containers stored at 5–25 °C retain specification-level PSD and pH for 12–18 months. Freeze–thaw cycling is explicitly outside operational boundaries: ice crystal growth ruptures the dispersant shell and produces irreversible hard agglomerates that cannot be redispersed by agitation. Storage above 35 °C is avoided because dissolved CO₂ ingress accelerates pH drift and promotes microbial growth in formulations without biocides. Sedimentation during static storage is expected and reversible; redisversion is accomplished with 30–60 min of low-shear recirculation, followed by PSD verification per ISO 13320:2020. High-density polyethylene containers are specified over glass or unlined steel because glass leaches sodium and steel introduces iron above the 10 ppm acceptance limit. Preservative additives, where used, are selected for compatibility with subsequent metal deposition; amine-based biocides are explicitly excluded because they adsorb onto alumina surfaces and shift zeta potential below the |30 mV| dispersion-stability threshold.

    Removal Rate Benchmarks Vary by Substrate Crystallography

    Removal rate is not a single-valued material constant. On c-plane (0001) sapphire, EL-grade alumina typically removes 2–6 μm/hr; on a-plane (11–20) and r-plane (1–102) orientations, rates fall to 1–3 μm/hr because crystallographic plane hardness varies with slip-system orientation. On 4H-silicon carbide, the Si-face (0001) is polished at 0.5–1.5 μm/hr with alumina, while the C-face (000–1) proceeds at approximately double that rate under identical parameters. Within-wafer non-uniformity (WIWNU, 1σ) is maintained below 5% on 100 mm sapphire wafers by adjusting carrier back-pressure, platen temperature, and slurry flow rate; uniformity is measured after polish by spectroscopic ellipsometry across a 49-point polar map. Batch-to-batch removal-rate variance of ±10% is observed across 200 L production lots when dispersant lot changes occur without re-qualification.

    Controlling pH Drift in High-Solids Slurries During Extended Runs

    Extended polish campaigns exceeding 8 h on recirculated slurry exhibit progressive pH drift caused by atmospheric CO₂ absorption, slow alumina dissolution, and accumulation of pad debris and substrate fines. A drop from pH 10.2 to pH 9.4 reduces zeta potential from −45 mV to −28 mV and triggers measurable agglomeration; a rise above pH 10.8 accelerates dispersant desorption and increases particle adhesion to the pad. In-line pH probes with automatic KOH dosing maintain the working band at 9.8–10.5, with titrant addition limited to <0.3 mL/min per 100 L bath volume. Pad debris is removed through the point-of-use filter, but filter loading follows an exponential rise after 6 h of sapphire polishing and the pressure differential must be trended rather than alarm-only monitored. Slurry bath life in recirculating tools is typically capped at 24 h to prevent cross-contamination between wafer lots, regardless of pH reading.

    Compliance and characterization matrix for EL-grade alumina slurry release.
    ParameterMethod / StandardAcceptance criterion
    Particle-size distributionISO 13320:2020D50 within ±10% of CoA value
    Nanoscale particle sizeASTM E2490-09replicate coefficient of variation ≤5%
    Specific surface areaISO 9277:2022, ASTM D3663-205–20 m²/g
    ViscosityASTM D21965–50 cP at 25 °C, 100 s⁻¹
    pHASTM E709.8–10.5 (alkaline grade)
    Trace metalsSEMI C1 ICP-MS<5 ppm per element
    Dilution waterSEMI F57, ASTM D1193-0618 MΩ·cm resistivity, 0.1 μm filtered
    Packaging environmentISO 14644-1:2015Class 5 at point of fill
    RoHS restricted substancesEU 2011/65/EU, Annex IInot intentionally added
    REACH SVHCEC 1907/2006<0.1 wt%

    After polishing, wafers exit the platen with a residual alumina film that must be removed before metrology or epitaxial growth. The standard cleaning sequence employs megasonic-assisted DI water at 40–50 °C, followed by a 1–2 wt% citric acid rinse at pH 2.5–3.0 to dissolve adsorbed alumina without attacking the sapphire substrate. Megasonic power density is capped at 5–10 W/cm² because higher acoustic intensities generate cavitation damage on 100 mm wafers with edge exclusion below 3 mm. Residual particle counts after cleaning, measured by a surface particle counter with 0.1 μm sensitivity, are held below 5 adders per wafer. Incomplete alumina removal manifests as haze on subsequent GaN MOCVD epilayers and is traceable to the post-CMP clean rather than to slurry composition itself.

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