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Nano Silica Polishing Slurry Electronic/EL Grade

    • Product Name: Nano Silica 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 128299
    Product Nano Silica Polishing Slurry Electronic/EL Grade
    Appearance Milky white uniform liquid
    Silica Content 30-40 wt%
    Average Particle Size D50 50-100 nm
    Ph Value 9.0-11.0
    Viscosity 25 C < 20 mPa·s
    Density 1.20-1.30 g/cm³
    Specific Gravity 1.20-1.30
    Metallic Impurity Level Na < 1 ppm, Fe < 0.1 ppm, Cu < 0.1 ppm
    Purity Grade Electronics/EL Grade
    Shelf Life 12 months
    Storage Temperature 5°C to 35°C

    As an accredited Nano Silica 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 1 L HDPE bottles, nitrogen-protected and tamper-evident sealed, labeled as Electronic/EL Grade Nano Silica Polishing Slurry.
    Container Loading (20′ FCL) 20′ FCL loading of Nano Silica Polishing Slurry (Electronic/EL Grade) in sealed, palletized drums, properly secured for safe transport.
    Shipping Ship Nano Silica Polishing Slurry (Electronic/EL Grade) in sealed HDPE drums with secure caps. Use clean, labeled containers. Maintain 5–35°C; avoid freezing, overheating, and direct sunlight to prevent agglomeration. Strap upright on pallets, protect from moisture and contaminants. Confirm SDS for DG classification; packaging must meet local transport regulations.
    Storage Store in a tightly sealed container to prevent contamination. Keep in a cool, dry area away from direct sunlight. Maintain temperature between 5–30°C, avoiding freezing or excessive heat. Use clean equipment to prevent particle aggregation. Ensure proper ventilation and label clearly. Shelf life is typically six months from manufacture if stored under recommended conditions.
    Shelf Life Shelf life is typically 6–12 months when stored sealed at 5–30°C, avoiding freezing, contamination, and direct sunlight.
    Application of Nano Silica Polishing Slurry Electronic/EL Grade
    In front-end-of-line shallow trench isolation processing at the 28 nm node and below, the colloidal silica slurry formulation directly governs the post-CMP silicon nitride selectivity window required to maintain trench dielectric integrity while achieving target silicon oxide removal rates. A concentrated electronic-grade slurry with 30 wt% SiO2 loading and a primary particle size distribution of 30–80 nm is diluted at the point of use with ultrapure deionized water in a 1:1 to 1:2 volumetric ratio, reducing effective abrasive content to 15–20 wt% and stabilizing pH within the 10.0–11.5 range typically buffered by potassium hydroxide or tetramethylammonium hydroxide. Removal rate on plasma-enhanced chemical vapor deposition tetraethyl orthosilicate oxide falls within 3000–6000 Å/min under an applied downforce of 3.0–5.0 psi (21–35 kPa), a platen rotational speed of 60–100 rpm, a carrier speed of 60–90 rpm, and a slurry flow rate of 150–300 mL/min dispensed onto a polyurethane pad stack comprising an IC1000 top pad over a Suba IV subpad. Silicon nitride removal under identical process conditions registers between 100–300 Å/min, yielding an oxide-to-nitride selectivity ratio of 20:1 to 50:1, which approaches 100:1 when ceria-doped colloidal silica formulations are introduced. Point-of-use filtration through a 0.5 μm depth filter maintains large particle counts below 50 particles/mL for particles exceeding 0.5 μm, while post-CMP cleaning in a megasonic-assisted dilute NH4OH or SC1 (APM) bath removes residual silica nanoparticles and pad debris. Defect inspection on a dark-field inspection tool at 90 nm sensitivity typically yields fewer than 10 micro-scratches per 300 mm wafer and fewer than 50 particle adders per wafer at a defect size threshold of 90 nm. The associated non-uniformity across the wafer diameter is specified below 3% one-sigma at an edge exclusion of 3 mm, while endpoint detection relies on motor-current shift or optical thickness monitoring to prevent over-polish of the underlying active region. Compliance on a 300 mm production line references SEMI S2-0720 for equipment safety, SEMI S8-0218 for ergonomic design, ISO 14644-1:2015 Class 1 cleanroom environment for slurry blending and dispense systems, and SEMI F57-0418 for trace metal contamination limits on silicon wafer surfaces. Equipment platforms include Applied Materials Reflexion LK and Ebara F-REX200/300 systems fitted with in-situ pad conditioning using a 3M A165 diamond disc conditioner operating at 9–12 lbf conditioning force. The end products fabricated through this STI CMP sequence include logic system-on-chip devices for smartphone application processors, graphics processing units, DRAM modules, and 3D NAND flash memory arrays. Published data from pad qualification campaigns indicates that pad break-in of 5–10 wafers is required before removal rate stabilizes within ±5% of target, while pad groove depth loss of 100–200 μm marks the pad-change threshold in high-volume production.

    When Copper Dishing Exceeds 30 nm at the 28 nm Node: What Limits the Barrier CMP Step Selectivity Window?

    The two-step copper interconnect chemical mechanical planarization sequence on a 300 mm production line separates bulk copper removal from diffusion barrier clearance because a single slurry formulation cannot simultaneously deliver the ≥3000 Å/min copper removal rate required for wafer throughput and the ≤200 Å/min Ta/TaN removal rate required to prevent low-k dielectric erosion within the back-end-of-line stack. Bulk copper slurry chemistry features colloidal silica at 1–5 wt%, hydrogen peroxide at 0.5–2 wt% supplied through a separate additive line to prevent decomposition-induced pH drift, glycine at 0.1–1 wt% as a copper complexing agent, and benzotriazole at 0.01–0.1 wt% to suppress isotropic copper corrosion and control static etch rate below 50 Å/min as measured by four-point probe sheet resistance delta. Barrier slurry chemistry shifts to colloidal silica at 5–10 wt% with pH adjusted to 9.0–11.0 using potassium hydroxide or amine-based buffers, and hydrogen peroxide optionally present at 0.5–1.0 wt% to accelerate tantalum nitride surface oxidation. The selectivity requirement derives from the 2 nm ultra-low-k dielectric hardmask budget remaining after barrier clear; excessive dielectric loss shifts interline capacitance and degrades RC delay at the 28 nm node where the minimum dielectric spacing between adjacent copper lines is 56 nm and the final post-CMP copper surface roughness must remain below 5 Å Ra as measured by AFM over a 10×10 μm scan area. Compliance for slurry chemical constituents follows REACH Regulation (EC) No 1907/2006 Annex XVII restrictions on classified substances, RoHS Directive 2011/65/EU substance limitations for lead, cadmium, and mercury at less than 1000 ppm by weight in homogeneous material, and SEMI S23-0716 energy utilization benchmarking for the CMP platform. The final barrier CMP process produces copper dishing of less than 30 nm on a 100×100 μm bond pad structure and dielectric erosion of less than 100 Å on a wide 50 μm feature, with removal rate on thermal silicon oxide for the barrier step registering 100–500 Å/min and copper removal during barrier over-polish limited to 100–600 Å/min to prevent excessive dishing on dense array regions. Post-barrier clean uses a two-step sequence of alkaline neutralizing clean followed by dilute citric acid chelating clean at 0.5–2 wt% concentration to remove copper-benzotriazole complexes from the wafer surface. The following comparative parameter matrix documents the systematic differences between the two slurry platforms.
    ParameterBulk Cu SlurryBarrier Slurry
    Colloidal silica loading1–5 wt%5–10 wt%
    Operating pH7.0–9.09.0–11.0
    H2O2 concentration0.5–2 wt%0.5–1.0 wt%
    Corrosion inhibitorBTA 0.01–0.1 wt%Not typically used
    Cu removal rate3000–8000 Å/min100–600 Å/min
    Ta/TaN removal rate<50 Å/min200–800 Å/min
    Low-k dielectric RR<20 Å/min100–500 Å/min
    Target dishing on 100×100 μm padN/A (bulk step)<30 nm
    Post-CMP Cu surface roughness<10 Å Ra<5 Å Ra
    Static etch rate<50 Å/min<20 Å/min
    End products at this stage include the complete copper/low-k back-end-of-line interconnect stack for high-performance computing processors, network ASICs, and advanced FPGA devices where the number of metal layers ranges from 8 to 15 and via pitch at the lowest levels reaches 56 nm. Defect budgets for the barrier CMP step specify fewer than 30 post-CMP defects per 300 mm wafer at a 90 nm detection threshold, with scratch counts held below 5 per wafer due to the known sensitivity of subsequent copper seed deposition to surface discontinuities of even 1–2 nm depth. The hydrogen peroxide supply line requires point-of-use filtration at 0.2 μm and concentration monitoring by UV absorbance at 240 nm to maintain the specified 0.5–2 wt% window, since decomposition of H2O2 in storage tanks decreases oxidizer availability and narrows the bulk copper removal rate operating envelope over a 24-hour production shift.Hexagonal silicon carbide substrate finishing presents a measurable material removal rate differential of approximately 2–4× between the silicon-terminated (0001) face and the carbon-terminated (000-1) face when polished with colloidal silica under identical downforce and platen speed conditions, a consequence of differing surface oxidation kinetics and hydration layer formation rates on each crystallographic plane. A concentrated electronic-grade slurry of 10–30 wt% SiO2 with primary particles of 20–50 nm and pH 8.0–11.0 is applied at a flow rate of 50–150 mL/min onto a soft polyurethane or non-woven pad affixed to a rotary polisher, with hydrogen peroxide at 2–5 wt% or potassium permanganate at 0.1–0.5 wt% introduced as an oxidant to accelerate surface oxide formation on the Si-face where material removal rates otherwise remain below 100 nm/hr. Published data for 4H-SiC (0001) Si-face CMP indicates removal rates of 50–200 nm/hr, while the C-face achieves 200–500 nm/hr under equivalent conditions; the slower Si-face rate imposes a significantly longer polishing cycle for 150 mm wafers requiring the removal of 2–5 μm of sub-surface damage generated during prior diamond mechanical polishing. Process parameter optimization therefore centers on achieving a trade-off between removal rate and surface step-terrace morphology retention, with AFM measurements at 5×5 μm scan area targeting RMS roughness below 0.2 nm and terrace width uniformity within ±10% across the wafer diameter. The compliance framework for silicon carbide substrate polishing references SEMI M81-0218 for 4H-SiC substrate diameter, thickness, bow, warp, and surface orientation specifications, alongside JEDEC JEP179 for power device reliability testing requirements and AEC-Q101 for automotive-grade qualification of discrete power semiconductors. Equipment typically comprises single-wafer or batch rotary CMP platforms retrofitted with high-hardness pad stacks and independent temperature control maintaining platen temperature below 30 °C to prevent slurry gelation from evaporative concentration. Post-CMP cleaning requires SC1 (APM) in a megasonic tank followed by piranha (H2SO4 : H2O2 at 3:1 volumetric ratio) to remove residual permanganate species and organic pad debris, with final rinsing in ultrapure water of resistivity exceeding 18.2 MΩ·cm. End products fabricated on polished 4H-SiC substrates include 1200 V trench MOSFETs for electric vehicle traction inverters, 1700 V Schottky barrier diodes for industrial motor drives, and 3.3 kV devices for photovoltaic inverter and railway traction applications. The polished substrate surface must support subsequent epitaxial growth with a defect density below 1 cm⁻² at a 100 nm detection threshold, as specified in device manufacturer qualification documents; substrates failing this criterion are rejected at incoming inspection using Candela CS920 or equivalent surface defect metrology systems operating at 0.3 μm sensitivity.

    If Sapphire Substrates Must Achieve Ra ≤ 0.2 nm Before GaN MOCVD Deposition

    Single-crystal sapphire substrate fabrication for gallium nitride epitaxy requires a sequential lapping and chemical mechanical planarization chain because the material's 9 Mohs hardness and anisotropic chemical reactivity preclude single-step stock removal from as-cut wafers. The CMP stage uses colloidal silica at 10–25 wt% SiO2 with a particle size distribution of 30–80 nm and pH 9.0–11.0 adjusted with potassium hydroxide or sodium hydroxide, dispensed at 100–300 mL/min onto a hard polyurethane pad rotating at 50–90 rpm with a downforce of 2.5–5.0 psi (17–35 kPa). Removal rate on c-plane (0001) sapphire ranges from 2–5 μm/hr depending on slurry temperature and pad conditioning state, while a-plane (11-20) and r-plane (1-102) orientations exhibit 10–30% lower removal rates under identical conditions due to differences in surface hydration layer formation. The sub-surface damage layer generated by the preceding diamond lapping step typically extends to a depth of 10–40 μm, so the CMP process must remove sufficient material to expose a damage-free surface that will not propagate threading dislocations into the subsequent GaN epitaxial layer. Compliance anchors to GB/T 31370.2-2015 for sapphire substrate specifications in LED applications, SEMI HB7 for sapphire substrate dimensions and surface quality, and IATF 16949 for automotive-grade LED supply chain quality management. Post-CMP annealing at temperatures above 1000 °C in a controlled atmosphere relieves residual polishing stress and eliminates sub-nanometer surface damage not detectable by conventional AFM imaging over a 10×10 μm scan area. Final substrate evaluation employs laser interferometry for total thickness variation control below 5 μm on a 150 mm diameter substrate and below 2 μm on a 100 mm substrate, while bow is maintained below 10 μm and surface roughness is verified below 0.2 nm Ra by AFM over a 5×5 μm scan area with the measurement iterated at five points across the wafer diameter. The end products fabricated on polished sapphire substrates include InGaN multi-quantum-well light-emitting diode epi-wafers for general illumination and automotive headlamps, AlGaN-based UV-C LED substrates for water purification and surface disinfection, and silicon-on-sapphire RF device substrates where the insulating sapphire base suppresses substrate coupling effects. Published data from LED epi-wafer manufacturers indicates that a substrate surface roughness increment from 0.1 nm to 0.3 nm raises the achievable internal quantum efficiency variance by approximately 5–15 percentage points across an epi-wafer batch, an observation that sustains the tight Ra ≤ 0.2 nm requirement and drives continuous monitoring of slurry particle size drift during production campaigns extending beyond 200 wafers per slurry charge.

    Optical Connector End-Face Geometry and the Colloidal Silica Finish Standard

    Polishing of a cylindrical zirconia ferrule containing an embedded single-mode optical fiber demands simultaneous material removal from two dissimilar materials with Vickers hardness values of approximately 1200 HV (zirconia) and 650 HV (fused silica), where differential removal leads to fiber undercut or protrusion that directly terminates a device's optical return loss performance envelope. The final polishing stage uses a colloidal silica slurry with 5–15 wt% SiO2, particle size 20–60 nm, and pH 9.0–11.0 applied to a compliant synthetic abrasive pad, following a sequence of diamond lapping films with abrasive grades descending from 9 μm to 1 μm and finally 0.5 μm diamond. Fiber protrusion or undercut relative to the ferrule end face is maintained within −100 nm to +50 nm per Telcordia GR-326-CORE Issue 4 Section 4.4.4, while radius of curvature spans 7–25 mm and apex offset remains below 50 μm as specified in IEC 61300-3-35:2015. Angled physical contact connectors require a pre-angled ferrule geometry of 8° ±0.2° and exhibit a return loss specification exceeding 60 dB after polishing, whereas ultra-physical contact connectors require a return loss exceeding 50 dB. A single polishing sequence processes the ferrule in a dedicated jig on a four-station polishing machine operating at a rotational speed of 30–80 rpm with a polishing time of 30–90 seconds for the colloidal silica final finish. The compliance matrix for this application includes IEC 61300-3-35:2015 for end-face visual inspection criteria, IEC 61755-2-1 for single-mode connector optical interface standards, Telcordia GR-326-CORE Issue 4 for generic requirements of single-mode optical connectors, and ISO 14644-1:2015 Class 5 cleanroom conditions for end-face inspection after polishing. Point-of-use slurry filtration at 0.5 μm prevents large-particle-induced scratches that create optical scattering centers visible at 200× magnification under coaxial illumination. End products integrated into the polished connector assembly include LC duplex connectors for data center fiber optic distribution, SC connectors for FTTH network drop cables, E2000 connectors with protective shutter for WDM network equipment, and MPO multi-fiber connectors for parallel optical interconnects at 40 Gbps and 100 Gbps transmission rates. Field failure analysis data from network operators indicates that a fiber undercut exceeding −50 nm correlates with a return loss degradation of 5–10 dB after 500 mating cycles, which anchors the geometry tolerance window in manufacturing statistical process control limits and prohibits slurry substitution without full re-qualification of the polishing recipe.In through-silicon via integration for 3D stacked memory and logic devices, the chemical mechanical planarization step following wafer backgrind performs two distinct functions: selective removal of copper overburden to expose via structures, and planarization of the interlayer dielectric in redistribution layer build-up. The copper reveal CMP step on a 300 mm wafer uses a colloidal silica slurry at 1–5 wt% SiO2 with pH 7.0–9.0, hydrogen peroxide at 0.5–2 wt% from an independent additive line, and corrosion inhibitor concentrations tuned to maintain static etch rate below 30 Å/min because the post-reveal copper surface becomes the direct bonding interface for subsequent backside passivation deposition. Copper removal rate spans 2000–5000 Å/min with a dishing specification of less than 30 nm on TSV arrays with via diameters of 5–10 μm and via pitch of 10–40 μm, a constraint that becomes increasingly difficult as via density increases because pad bending and slurry transport limitations create local removal rate disparities between via field edges and centers. The subsequent dielectric CMP step for redistribution layer planarization employs colloidal silica at 10–25 wt% SiO2 with pH 10.0–11.5 and removal rate on PECVD silicon oxide of 1000–3000 Å/min, requiring high selectivity to the underlying copper pillars and bump structures that must not exhibit excessive top surface recession before solder bump or copper pillar attachment. Equipment for TSV CMP includes Applied Materials Reflexion LK systems configured with multi-zone carrier pressure control for compensating edge-fast removal profiles observed at the 2 mm wafer-edge exclusion zone, and Okamoto single-wafer polishers for lower-volume production environments. Slurry delivery requires a dual-line point-of-use blending system that mixes concentrated abrasive with ultrapure water and oxidizer at controlled ratios, with filtration at 0.5 μm and slurry temperature maintained at 20–25 °C to prevent removal rate drift exceeding ±5% across a 25-wafer lot. Compliance references JEDEC JESD235:2016 for design guidelines for 3D stacked integrated circuits, SEMI 3D-IC Committee documents for TSV depth and diameter metrology standards, and IPC-7095 for assembly-level reliability requirements after package stacking. The parameter matrix below consolidates the critical CMP conditions for TSV reveal and RDL planarization.
    ParameterTSV Cu Reveal CMPRDL Dielectric CMP
    Slurry typeColloidal silica + H2O2 + inhibitorAlkaline colloidal silica
    Abrasive loading1–5 wt% SiO210–25 wt% SiO2
    Operating pH7.0–9.010.0–11.5
    Downforce2.0–4.0 psi2.5–4.5 psi
    Platen / carrier speed60–80 / 50–70 rpm60–90 / 60–90 rpm
    Slurry flow rate150–250 mL/min150–300 mL/min
    Target removal rate2000–5000 Å/min1000–3000 Å/min
    Dishing target (5–10 μm via)<30 nmN/A
    Edge exclusion2 mm3 mm
    Defect budget (>0.5 μm)<50 adders per wafer<50 adders per wafer
    Slurry temperature20–25 °C20–25 °C
    End products fabricated through this integration include high-bandwidth memory stacks with 8 or 12 DRAM layers interconnected through TSVs, 2.5D silicon interposers with multiple chiplets mounted side by side, and chiplet-based processors where TSV CMP enables direct copper-to-copper hybrid bonding with interconnect pitch below 10 μm. Published data from packaging foundries indicates that TSV copper dishing increases approximately 10–15 nm per 100 μm of via pitch reduction below 20 μm pitch, which requires iterative adjustment of slurry flow rate and platen speed during process qualification and precludes direct transfer of a qualified recipe from a 40 μm via-pitch product to a 10 μm via-pitch product without re-optimization. The backgrind-to-CMP delay window after wafer thinning is typically specified at less than 4 hours due to time-dependent copper oxide growth on exposed vias, which shifts the CMP removal rate by 10–20% if exceeded. Post-CMP metrology employs white-light interferometry for copper dishing mapping across a 49-point polar array sampling scheme and atomic force microscopy for local surface roughness verification at 1×1 μm scan area on via tops.

    Photomask Substrate Flatness Control at 0.5 μm Total Indicator Reading on 6025 Quartz

    Synthetic fused silica mask blank substrates of 152.4 mm × 152.4 mm × 6.35 mm (6025 format) constitute a low-defect application where the colloidal silica slurry must deliver sub-nanometer surface roughness while maintaining total indicator reading flatness below 0.5 μm over the 142 mm × 142 mm quality area specified in SEMI P1-2318. The polishing process uses a high-purity colloidal silica slurry at less than 5 wt% SiO2 with a tight particle size distribution centered at 20 nm or below, dispensed at low flow rates of 20–50 mL/min onto a soft polyurethane or synthetic suede pad affixed to a double-sided polishing machine that processes both substrate faces simultaneously to preserve flatness symmetry. Removal rate on synthetic fused silica ranges from 0.5–2 μm/hr depending on pad hardness and slurry chemistry, deliberately low to prevent flatness degradation from edge-localized material loss that manifests as roll-off beyond the 0.5 μm TIR criterion when removal rates exceed 2 μm/hr on six-head double-sided machines. Surface roughness after final polish measures below 0.15 nm RMS by AFM over a 1×1 μm scan area, while laser interferometry confirms flatness at the 0.5 μm TIR specification across the quality area with a 49-point measurement grid excluding a 10 mm peripheral zone. The substrate must pass a post-polish defect inspection at a 0.5 μm optical defect size threshold, with fewer than 5 adders per substrate acceptable for advanced photomask applications and zero defects allowed above 1 μm in size. Compliance for mask blank polishing anchors to SEMI P1-2318 for hard surface photomask substrate dimensions, flatness, and surface quality, SEMI P30 for photomask blank requirements at 193 nm immersion lithography, and ISO 10110 for optical element surface quality notations. Slurry purity requirements demand cation concentrations below 10 ppb for sodium, potassium, iron, and copper, with chloride below 50 ppm and total organic carbon below 50 ppm, verified by ICP-MS analysis per slurry lot with full traceability to raw silica sol production batch records. End products fabricated on these polished substrates include attenuated phase-shift mask blanks for 193 nm immersion lithography at 28–7 nm nodes, binary photomask blanks for mature-node production, and extreme ultraviolet mask blanks where the low thermal expansion substrate forms the base for molybdenum/silicon multilayer reflective coatings. Published data for EUV mask blank flatness requirements indicates that the multilayer deposition step imposes a total flatness deviation of less than 50 nm over a 50 mm square area, an order of magnitude tighter than the substrate-level specification, so the polishing process must achieve a surface quality that survives multilayer coating without distortion accumulation exceeding 10 nm per deposition run. Post-polish storage conditions for polished quartz substrates specify a relative humidity below 50% and a particle-controlled environment of ISO 14644-1:2015 Class 4 or better to prevent water-spot formation on the polished surface during the interval between final cleaning and photoresist coating.
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    Certification & Compliance
    More Introduction

    Electronic/EL grade nano silica polishing slurry is supplied as an aqueous dispersion of amorphous silica nanoparticles with a supplier reference model designated EL-30. The dispersion is formulated at 30.0 ± 0.5 wt% SiO₂, with a pH of 10.0–10.8 at 25 °C, and a mean hydrodynamic diameter of 30–45 nm determined by dynamic light scattering in accordance with ISO 22412:2017. The product is intended for chemical mechanical planarization (CMP) of silicon dioxide interlayer dielectrics, shallow trench isolation (STI) structures, and polysilicon stop-on-nitride applications in front-end semiconductor fabrication. The EL grade differs from general-purpose colloidal silicas through a lower cation contamination ceiling and a tighter large-particle tail, both of which are controlled to reduce post-polish defect density on patterned wafers.

    Representative EL-30 grade certificate-of-analysis acceptance windows
    PropertyTest methodAcceptance value
    Silica solidsGravimetric desiccation at 120 °C30.0 ± 0.5 wt%
    pH at 25 °CASTM E70-2210.0–10.8
    Dynamic viscosity at 25 °C, 100 s⁻¹ASTM D2196-20≤ 5.0 mPa·s
    Mean hydrodynamic diameterISO 22412:201730–45 nm
    D99 hydrodynamic diameterISO 22412:2017≤ 80 nm
    SodiumICP-MS, EPA 6020B≤ 100 ppb
    PotassiumICP-MS, EPA 6020B≤ 100 ppb
    Total transition metals: Fe, Cr, Ni, Cu, ZnICP-MS, EPA 6020B≤ 100 ppb combined
    ChlorideIon chromatography, EPA 300.1≤ 1 ppm
    Large particle count at ≥ 0.5 µmLight obscuration, Rion KS-41A≤ 500 particles/mL

    In the as-supplied condition, the slurry remains electrostatically stabilized at pH 10.0–10.8, producing a zeta potential generally below −30 mV measured by electrophoretic light scattering using a Malvern Zetasizer Nano ZS at 25 °C. Continuous recirculation in the distribution loop is required when the product remains in a production line for more than 8 h; dead-legs in stagnant piping can accumulate large particles and increase defect counts. Point-of-use filtration is specified at 0.5 µm or 0.2 µm with polypropylene or PVDF filter capsules. Nylon membranes are unsuitable because the alkaline pH degrades the membrane and releases extractable amines. Filtration pressure should not exceed 50 kPa differential to avoid filter cake compaction and particle breakthrough.

    What process envelope governs oxide removal rate on commercial CMP platforms?

    Oxide removal rate with the EL grade is process-dependent and is typically evaluated on rotary polishers such as the Applied Materials Mirra/Reflexion or Ebara FREX platforms. Representative conditions include a downforce of 2.0–4.0 psi, platen speed of 60–110 rpm, head speed of 55–105 rpm, and slurry flow of 100–200 mL/min. On a cast polyurethane pad with Shore D hardness between 52 and 58 as measured by ASTM D2240, the material removes PECVD TEOS oxide at rates that typically remain within 200–500 nm/min, depending on pad conditioning and wafer pattern density. The removal rate increases approximately linearly with downforce between 1.5 psi and 4.0 psi; above 4.5 psi, the response plateaus as the system enters mixed-lubrication rather than hydrodynamic contact. The slurry is not formulated with an oxidizer, so removal on silicon nitride stop layers is low; this property provides a polishing selectivity window of 3:1 to 5:1 oxide-to-nitride on blanket wafers, but the exact ratio is mask-pattern-dependent.

    In shallow trench isolation polishing, the critical defect source is not the mean particle size but the large-particle tail. The EL grade is controlled at a D99 value of ≤ 80 nm by ISO 22412:2017 and an optical large-particle count of ≤ 500 particles/mL at ≥ 0.5 µm using light obscuration. On a production line, excursions above 2,000 particles/mL at ≥ 0.5 µm have been observed to correlate with microscratch counts on blanket oxide monitors, particularly after pad glazing or point-of-use dilution with deionized water of insufficient alkalinity. To maintain the particle size distribution, dilution should use only semiconductor-grade ultrapure water meeting ASTM D5127-13, with the pH pre-adjusted to 9.0–10.0 by ammonium hydroxide. Dilution without pH adjustment can reduce the zeta potential and cause silica aggregation in the supply line.

    When slurry purity determines post-CMP defect density

    Post-CMP defect density on logic and memory devices is governed by residual metal contamination, organic residues, and sub-surface damage. The EL grade is manufactured through cation-exchange treatment after sol-gel synthesis, which reduces the total transition metal burden to ≤ 100 ppb combined for iron, chromium, nickel, copper, and zinc as determined by ICP-MS using EPA 6020B. Sodium and potassium are separately controlled at ≤ 100 ppb each. Chloride is maintained below 1 ppm by ion chromatography using EPA 300.1. These ceilings are relevant for gate-oxide integrity and mobile-ion drift; a sodium concentration above approximately 1 × 10¹² atoms/cm² on a pre-diffusion wafer surface is an established reliability concern in MOS devices. Because the slurry leaves a trace silica film after drying, post-CMP cleaning with dilute ammonium hydroxide or tetramethylammonium hydroxide is required to remove residual particles before subsequent dielectric deposition.

    Comparative profile of EL-30 grade nano silica, conventional colloidal silica, and fumed silica
    ParameterNano silica EL-30Conventional colloidal silicaFumed silica
    Synthesis routeAqueous sol-gel, cation-exchangedAqueous sol-gelPyrogenic hydrolysis of silicon tetrachloride
    Mean particle size30–45 nm20–80 nm7–40 nm primary; aggregates commonly exceed 100 nm
    Large-particle tailD99 ≤ 80 nm; controlled LPCModerate, supplier-dependentHigh aggregate fraction unless energy-dispersed
    Transition metal level≤ 100 ppb combined100–1,000 ppb typicalOften 1,000–5,000 ppb before purification
    Oxide CMP defectivityLower microscratch density on polyurethane pads at pH 10.5BaselineHigher scratch risk unless aggregate dispersion is maintained
    Sealed shelf life≥ 12 months at 5–35 °CSimilarCan settle or gel after freeze-thaw cycling
    Operating pH range10.0–10.88.5–11.02.5–4.0 or alkaline after dispersion

    Differences from conventional colloidal silica are expressed mainly in the large-particle count and cation levels. General-purpose colloidal silica can contain transition metals in the 100–1,000 ppb range and elevated aluminum residues, whereas the EL grade is processed to lower these contaminants. Fumed silica dispersions, although available at small primary particle sizes, contain hard aggregates that require high-shear dispersion. Under production-scale CMP conditions, fumed silica slurries may show higher microscratch densities unless the aggregate fraction is reduced by milling or high-energy mixing. Compared with ceria slurries, the EL grade has lower intrinsic hardness and may not achieve the same silicon nitride removal rate in advanced STI applications; however, the softer silica surface offers a lower scratch propensity on oxide and low-k dielectric films. Compared with alumina slurries, silica provides lower defectivity on silicon dioxide, but its removal rate on silicon nitride is also lower, which requires process-specific selectivity tuning through pad selection and downforce.

    For copper damascene and tungsten contact polishing, the EL grade is not intended as a metal removal slurry because it lacks the oxidizers and corrosion inhibitors necessary for copper or tungsten CMP. It may be applied as a dielectric buff after barrier CMP to remove residual oxide and improve surface roughness. Mixing with acidic peroxide-based metal CMP slurries should be avoided unless the lines are flushed completely; residual silica can gel in acidic oxidizer media and create particles. The product should be stored between 5 °C and 35 °C in sealed containers. Freeze-thaw cycling causes irreversible agglomeration. Contact with aluminum sulfate, cationic polyelectrolytes, or strong acids below pH 2.0 destabilizes the dispersion. The product should not be frozen, and any material that has been exposed to freezing must be discarded rather than filtered and reused.

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