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Nano Silica Abrasive Powder Electronic/EL Grade

    • Product Name: Nano Silica Abrasive Powder 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 641189
    Purity 99.99
    Average Particle Size Nm 30-50
    Specific Surface Area M2 G 150-250
    Ph 5 Aqueous Solution 6.5-7.5
    Moisture Content <=0.5
    Loss On Drying <=1.0
    Ignition Loss <=1.5
    Chloride Content Ppm <=10
    Iron Content Ppm <=5
    Heavy Metals Content Ppm <=10
    Crystal Form Amorphous
    Sio2 Content >=99.9
    Refractive Index 1.46
    Mohs Hardness 7
    Morphology Spherical

    As an accredited Nano Silica Abrasive Powder 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 sealed 1 kg HDPE bottles with tamper-evident caps, labeled for Electronic/EL grade purity and safe handling.
    Container Loading (20′ FCL) 20′ FCL loading: Electronic/EL Grade Nano Silica Abrasive Powder in sealed, palletized drums/bags, safely secured for transit.
    Shipping This electronic/EL-grade nano silica powder is shipped in moisture-resistant sealed bags inside sturdy fiber drums to prevent contamination. Suitable for air, sea, or ground freight and not classified as dangerous goods. Store in a cool, dry area away from humidity during transit.
    Storage Store Nano Silica Abrasive Powder (Electronic/EL Grade) in a sealed, moisture-proof container in a cool, dry, well-ventilated area. Keep away from humidity, direct sunlight, and incompatible substances. Avoid dust generation and contamination. Maintain ambient temperature and low humidity; use within recommended shelf life to preserve purity and particle performance.
    Shelf Life Shelf life is typically two years when stored unopened in a cool, dry environment, maintaining optimal performance.
    Application of Nano Silica Abrasive Powder Electronic/EL Grade

    During shallow trench isolation and interlayer dielectric planarization in logic device manufacturing, the electronic-grade nano silica abrasive is incorporated into oxide CMP slurry formulations as the primary inorganic removal component. The as-received powder is dispersed as a 30–50 wt% stock, then diluted with ultrapure water to a final point-of-use solids loading of 8–15 wt%. Particle size is controlled to a modal diameter of 60–80 nm by dynamic light scattering per ISO 22412:2017, with a D90 below 120 nm and a large particle count above 0.2 µm below 1,000 particles/mL for a 100 mL sample. Trace metal specifications for this grade require sodium, potassium, iron, copper, and aluminum each below 10 ppb after 1:5 dilution, because cationic impurities above 50 ppb can shift zeta potential from -35 mV toward the isoelectric point and induce shear-thinning instability. The working pH is buffered with potassium hydroxide or ammonium hydroxide to pH 10.0–11.5; below pH 9.5, the silicon dioxide surface hydration rate decreases and oxide removal drops by more than 30% in production-scale trials on 300 mm wafers.

    On a rotary CMP system with a hard polyurethane pad, such as an Applied Materials Reflexion LK or Ebara F-REX 300, the slurry is supplied at 100–250 mL/min with table speed 30–80 rpm, membrane pressure 2.0–4.0 psi, and retaining ring pressure 2.5–5.0 psi. Under these conditions, thermal oxide removal rates of 150–300 nm/min are typical for blanket 100 mm coupon tests with within-wafer non-uniformity below 3%. The nano silica particles generate a hydrated silanol-rich layer on the dielectric surface; that layer is abraded by pad asperities while the alkaline chemistry continuously re-exposes silanol groups. If abrasive loading exceeds 18 wt%, glaze formation on the pad surface increases and removal rate plateaus while total defect count rises above 50 counts/wafer on post-CMP laser inspection. If loading falls below 5 wt%, removal becomes pad-pressure-limited and edge-to-center non-uniformity increases. The operational window therefore sits within a narrow composition band, and pre-filtration through a 0.5 µm point-of-use filter is required to remove agglomerates. The slurry pot must be recirculated continuously because stagnant zones produce large particle spikes after 4 h. The terminal product is a planarized STI or ILD layer on 300 mm silicon wafers ready for subsequent CVD and photolithography steps.

    Slurry conditionSolids loadingD50 after 7 daysThermal oxide removal rateLarge particle count > 0.2 µm
    Baseline pH 10.5, 3.0 psi, 60 rpm5 wt%62 nm120–150 nm/min<500 particles/mL
    Baseline pH 10.5, 3.0 psi, 60 rpm10 wt%64 nm180–220 nm/min<700 particles/mL
    Baseline pH 10.5, 3.0 psi, 60 rpm15 wt%67 nm230–280 nm/min<900 particles/mL
    Baseline pH 10.5, 3.0 psi, 60 rpm20 wt%71 nm250–290 nm/min1,500–2,000 particles/mL

    What Limits Edge-to-Center Non-Uniformity in Sapphire Wafer Polishing?

    For epi-ready sapphire substrate polishing after diamond mechanical lapping and post-lapping annealing, the removal mechanism shifts from Al₂O₃ fracture-dominated wear to chemically assisted tribological removal enabled by silica particles in an alkaline slurry. The slurry is prepared at 20–35 wt% solids, with primary particle diameter between 80–120 nm; larger primary particles create crescent-shaped subsurface damage and increase haze after KOH etch inspection. The working pH is 10.5–11.5, maintained by sodium hydroxide or tetramethylammonium hydroxide, and the slurry temperature is held at 45–55°C because sapphire surfaces require thermal activation for synergetic dissolution and mechanical abrasion. Removal rates on c-plane sapphire from 0.8–2.5 µm/h are typical on single-side polishing machines with composite hard pads and diamond-conditioned carriers. A downforce of 30–60 g/cm² and platen speed of 20–40 rpm are used, with slurry recirculation through cooling coils to prevent evaporative thickening above 2% water loss per hour.

    Edge-to-center non-uniformity is controlled by pad deformation at the wafer edge, carrier back-pressure zoning, and slurry film replenishment at the wafer track. The center of a 4-inch sapphire wafer commonly exhibits a different rate than the annulus between 10–40 mm radius on production tools; rate deviation beyond 5% creates thickness runout exceeding 3 µm after 2 h and compromises epi-ready flatness for MOCVD. A compensating pressure template with 400 g/cm² edge load and 280 g/cm² center load is typical on copper or stainless carriers. The slurry must be filtered to 1 µm at the point of delivery, and peristaltic pumps are preferred because centrifugal pumps generate shear above 1,000 s⁻¹ that can fracture particle aggregates and release sub-20 nm fragments that survive final brush cleaning. For LED-grade substrates, total metal contamination in the dried slurry residue must be below 10 ppb for Fe, Ni, Cu, and Zn, because residual metals reduce radiative recombination in quantum wells. The terminal product is a single-side or double-side polished sapphire wafer with surface roughness below 0.3 nm Ra over 5 µm × 5 µm AFM scans and total thickness variation below 5 µm for 2-inch and 4-inch diameters.

    Low-pH Silica Slurries Clear TaN Barrier Films in Damascene Structures

    After electrochemical copper plating and bulk copper removal in dual-damascene processing, the barrier layer of tantalum/tantalum nitride is cleared with an abrasive slurry formulated from the same electronic-grade silica powder, but at lower pH and modified with corrosion inhibitors. The powder is dispersed in deionized water at 2–8 wt% solids, adjusted to pH 5.5–7.5 with organic acid and hydrogen peroxide, because copper at alkaline pH forms insoluble hydroxide precipitates that redeposit on patterned wafers. A typical formulation includes 5 wt% silica at 60 nm primary particle size, 0.5–1.5 wt% hydrogen peroxide from 30% stock, and 0.1–0.5 wt% benzotriazole or 1,2,4-triazole as copper inhibitor. Abrasive concentration is lower than in oxide CMP because the barrier film thickness is usually 5–25 nm and excess mechanical energy damages low-k dielectrics at pattern densities above 60%.

    On 300 mm CMP tools with soft poromeric pads, downforce is reduced to 1.0–2.5 psi, and platen speed is set to 60–110 rpm to limit shear-induced copper recess. Endpoint signal is captured by eddy-current or optical reflectance; clearing of TaN is observed as a reflectance drop of 10–20% at 670 nm. If the silica particle count exceeds 8 wt%, dielectric erosion increases by more than 25% on isolated structures, and if the pH drops below 5.0, the zeta potential of silica approaches near-neutral values and slurry stability degrades within 30 min. Slurry pot residence time must not exceed 8 h because hydrogen peroxide decay of 0.05–0.15 wt% per hour shifts selectivity and copper oxide dissolution. Filtration with a 0.5 µm absolute-rated filter is set at 50–100 mL/min per liter of slurry. Batch-to-batch variation in silica surface silanol density is controlled by titration to less than 0.2 mmol/g to maintain removal selectivity between copper and TaN. The terminal product is a fully planarized damascene interconnect or TSV liner with copper loss below 10 nm per wafer pass and dielectric roughness increase below 0.5 nm Ra after barrier clear.

    In power and RF device substrate manufacturing, the mechanical hardness of single-crystal silicon carbide produces unacceptable subsurface damage when conventional diamond or alumina abrasives are used; the electronic-grade nano silica abrasive is therefore applied after a thermal oxidation step that converts the SiC surface to a softer silicon dioxide layer. The wafer is oxidized in a diffusion furnace at 1050–1250°C for 2–8 h to grow 50–200 nm of sacrificial oxide, after which a silica-based polish removes the oxide and a controlled thickness of underlying SiC by chemically assisted tribological action. The slurry is prepared at 10–20 wt% solids with particle size 40–70 nm, pH 9.5–10.5, and is delivered at 1–2 L/min to a rigid platen polisher with a 12-inch carrier. Head pressure in the range of 200–500 g/cm² is applied; above 500 g/cm², a brittle-to-ductile transition is exceeded and subsurface crack density increases by a factor of 5 on (0001) Si-face wafers.

    Removal rate on Si-face 4H-SiC after complete oxide consumption is 0.5–1.5 µm/h, intentionally low to avoid forming basal plane dislocations during stepped-terrace abrasion. The C-face is polished independently under the same chemistry because its oxidation rate is 3–5× higher and oxide thickness control is more sensitive. Post-polish characterization uses differential interference contrast microscopy, atomic force microscopy over 2 µm × 2 µm scans, and cross-sectional transmission electron microscopy to verify subsurface damage depth below 10 nm. The wafer must be cleaned immediately after polishing with a 0.1 wt% ammonium hydroxide solution and then piranha etchant at 4:1 H₂SO₄/H₂O₂ to remove silica residue before epitaxial growth. Metallic surface contamination must be below 5 × 10¹⁰ atoms/cm² by vapor phase decomposition inductively coupled plasma mass spectrometry; any residual Fe or Cu above 1 × 10¹¹ atoms/cm² degrades Schottky barrier uniformity. The terminal product is an epi-ready SiC substrate with Ra < 0.2 nm on the Si face and total thickness variation below 4 µm for 100 mm and 150 mm wafers.

    When Photomask Blank Substrates Require Sub-0.3 nm Sq Roughness

    Synthetic fused silica photomask blanks for ArF and EUV lithography demand surface finishes that cannot be achieved by cerium oxide polishing alone because ceria residue and subsurface cerium contamination reduce transmission at 193 nm. In the final polishing step, a low-alkalinity nano silica dispersion at 1–5 wt% solids and pH 7.5–9.0 is used to remove 1–10 nm of material and heal prior surface damage. The abrasive particle size is tightly distributed with a D50 of 20–40 nm; the D99 is kept below 80 nm because even one shallow scratch of 0.5 nm depth over 10 µm length creates phase defects in the patterned absorber layer. The slurry is prepared in a cleanroom classified at ISO 14644-1:2015 Class 1, filtered through 0.1 µm absolute-rated membranes, and delivered in single-pass mode, not recirculated, to avoid cross-batch abrasion from pad debris.

    Polishing is executed on a continuous pitch polisher with a closed-loop flatness control system; platen speed of 10–25 rpm and low downforce of 20–50 g/cm² prevent thermal gradients that produce local non-uniformity in the fused silica matrix. Surface roughness is quantified by white-light interferometry and AFM over 1 µm × 1 µm areas; root-mean-square roughness below 0.15 nm and peak-to-valley below 1.0 nm are typical for production blanks. The slurry pH and abrasive concentration are monitored by in-line electrical conductivity and density meters; a density drift of 0.002 g/cm³ indicates evaporation and triggers automatic make-up with ultrapure water. Residual silica particles on the substrate after polishing are removed by megasonic cleaning at 40–80 W and 0.5–1.0 MHz with dilute ammonia, followed by spin drying under filtered nitrogen. The final mask blank is characterized by surface roughness of 0.08–0.15 nm Rq and transmission loss below 0.2% at 193 nm after a 10 min UV exposure test.

    Glass Hard Disk Substrate NiP Overcoat Polishing with Silica Abrasives

    Electroless nickel-phosphorus plated aluminum substrates for perpendicular magnetic recording are planarized with a two-step silica slurry process that separates bulk removal from final finish control. The first step uses 8–12 wt% silica at 30–50 nm particle size and pH 2.5–4.0, adjusted with nitric acid, to remove 2–5 µm of NiP and reduce waviness from diamond milling. The second step drops abrasive loading to 2–5 wt% with 20–30 nm particles at pH 2.0–3.0 to produce a mirror finish without phosphate precipitation. The slurry is supplied at 50–150 mL/min to a double-side planetary polisher, typically a SpeedFam 32B or similar, with 50–150 gf/cm² pad pressure and 15–30 rpm upper and lower platen rotation.

    After chemomechanical polishing, surface roughness is measured by AFM over 5 µm × 5 µm scans to be below 0.2 nm Ra, and peak-to-valley roughness below 1.5 nm. The remaining NiP thickness after finishing is typically 8–12 µm, with total thickness variation less than 1 µm across a 95 mm disk. The process window is narrow because pH above 4.0 causes silica gelation and pad loading, while pH below 1.8 increases nickel dissolution and creates pit defects above 10 defects/disk under HDI inspection. The terminal product is a polished hard disk substrate with 95 mm or 65 mm diameter and surface finish suitable for sputtered magnetic layers.

    ParameterRelease limitTest methodStage
    Slurry particle size D5020–30 nmISO 22412:2017Each batch
    Large particle count > 0.5 µm<500 particles/mLOptical particle counterEach batch
    Slurry pH2.0–3.0ISO 787-9Each batch
    Trace metals Ni, Fe, Cu, Zn<10 ppb eachICP-MS after dissolutionEach batch
    Post-polish surface roughness<0.2 nm Ra over 5 µm × 5 µmAFM per ISO 25178-6Each lot
    Post-clean particle contamination<100 particles/disk over 0.2 µmISO 16232-4Each lot
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    Certification & Compliance
    More Introduction

    Nano Silica Abrasive Powder Electronic/EL Grade, model NS-EL-40, is a dry amorphous silicon dioxide abrasive produced for electronic-grade planarization and precision polishing. The powder consists of discrete, near-spherical primary particles with a transmission electron microscopy primary particle size of 20–50 nm. After high-shear dispersion in high-purity deionized water, the hydrodynamic D50 is typically 70–110 nm. The electronic/EL grade differs from optical-grade silica by the combination of total trace metal content below 50 mg/kg, a controlled large-particle count above 0.5 µm, and a narrow dispersed-particle distribution. The dry form is not a ready-to-use slurry; it requires predispersion at point of use, which permits solids loading to be adjusted between 5 wt% and 15 wt% without shipping water. This dry supply form reduces freight mass, limits microbial growth during storage, and allows powder shelf life to be managed independently from slurry aging.

    Release criteria for particle size, metal content, and dispersion pH

    The release specification is organized around three analytical boundaries: dry-powder dispersion behavior, trace contamination, and aqueous suspension chemistry. Acceptance requires all three boundaries to be met. A single out-of-range large-particle count or transition-metal result is sufficient to quarantine the lot from electronic polishing use.

    PropertyTypical release range or valueMethod
    Primary particle size, dry powder, TEM20–50 nmISO 21363:2020
    Dispersed hydrodynamic D5070–110 nmISO 22412:2017
    Dispersed hydrodynamic D90≤180 nmISO 22412:2017
    Specific surface area, BET60–120 m²/gISO 9277:2010
    pH at 5 wt% in DI water9.0–10.5ISO 10523:2008
    Total trace metals≤50 mg/kgISO 17294-2:2016
    Fe, Cu, Ni, Cr, each≤0.5 mg/kgISO 17294-2:2016
    Large-particle count >0.5 µm≤500 particles/mL at 1 wt%ISO 21501-4:2018
    Loss on drying, 105 °C, 2 h≤2.0 wt%ISO 787-2
    Residue on 45 µm sieve≤0.01 wt%ISO 787-7

    The powder is packaged in an ISO Class 5 cleanroom per ISO 14644-1:2015. Containers are purged with filtered dry nitrogen before sealing to limit moisture absorption and particle fallout onto the product surface.

    The pH window is a critical process limit. When pH falls below 8.0, the zeta potential measured by electrophoretic light scattering under ISO 13099-1:2012 drops below −20 mV, reducing electrostatic repulsion and increasing aggregate formation. Above 11.0, silica dissolution accelerates; continuous operation at pH 11.5 or higher can shift the dispersed D50 upward by 15–30 nm within 24 h as smaller particles dissolve and reprecipitate on larger surfaces. Therefore, the useful operating window for dielectric CMP is maintained at 9.5–10.8, with pH adjustment using semiconductor-grade KOH or NH₄OH.

    Dispersion conductivity should remain below 2.0 mS/cm for KOH-based systems. Above this value, the electrical double layer is compressed, and the suspension may exhibit shear-thickening behavior at solids loadings above 10 wt%. Inline conductivity monitoring with temperature compensation is recommended before slurry is released to the CMP tool.

    In chemical mechanical planarization, the dispersed powder functions as the mechanical abrasion component in the pad–wafer contact zone. On a production-scale rotary polisher with a polyurethane pad and in situ conditioning, slurry is supplied at 100–250 mL/min to a platen rotating at 60–90 rpm. Applied downforce is typically 3.0–6.0 psi for oxide interlevel dielectric and shallow trench isolation planarization. Under these conditions, a 10 wt% dispersion at pH 10.3 has produced blanket thermal-oxide removal rates of 220–380 nm/min on 200 mm wafers. Within-wafer non-uniformity remains below 4% across 49-point polar mapping when the platen temperature is controlled below 40 °C.

    The main process conflict is the trade-off between removal rate and post-clean defect density. Increasing solids loading above 12 wt% raises removal rate by approximately 15–25%, but large-particle count at the point of use increases nonlinearly unless filter area is also increased. At 15 wt%, a point-of-use 0.5 µm filter tends to load and may require twice the changeout frequency relative to 10 wt%. Post-CMP inspection on unpatterned oxide wafers indicates that large-particle counts above 1,000 particles/mL correlate with a sharp increase in dark-field micro-scratch counts. The release limit of ≤500 particles/mL at 1 wt% is therefore retained throughout the dispense line.

    Batch-to-batch variance in dispersed D50 is controlled to approximately ±10 nm. Because removal rate scales with available particle contact area, a shift from 80 nm to 100 nm D50 can alter blanket oxide removal rate by 5–10% under constant tool settings. Incoming lot qualification should therefore include dynamic light scattering D50, pH at 5 wt%, and large-particle count before release to the polishing bay.

    Point-of-use filtration is not optional. Without it, the large-particle count can exceed 2,000 particles/mL even after high-shear predispersion because partially wetted agglomerates break loose from tubing and fitting surfaces. Filter housing design should minimize dead legs; PTFE or high-density polyethylene wetted parts are preferred over EPDM seals that may shed.

    When electronic/EL grade silica powder replaces standard optical polishing silica

    Substitution of optical-grade silica in an electronic polishing process without requalification is not a simple drop-in. Optical-grade silica is commonly specified by median particle size and refractive index; electronic/EL grade adds a large-particle count threshold above 0.5 µm and trace-metal ceilings for iron, copper, nickel, and chromium. For electroluminescent or LED substrate polishing, alkali-metal contamination is especially constrained because sodium and potassium migrate under electrical bias and contribute to instability. The electronic/EL grade is supplied with total alkali metals below 10 mg/kg by ICP-MS; process water should meet ASTM D5127-13 Type E-1.2 to avoid reintroducing alkali after dispersion.

    AttributeElectronic/EL grade nano silica powderOptical-grade silicaFumed silica
    MorphologyDiscrete, near-sphericalIrregular crushed particlesFractal aggregates
    Dispersed D5070–110 nm150–300 nm>200 nm aggregated
    Total trace metals≤50 mg/kg100–300 mg/kg typicalMay exceed 500 mg/kg
    Large-particle count >0.5 µm≤500/mL at 1 wt%Not controlledHigh unless filtered
    Primary intended useCMP, LED/sapphire polishingOptical glass polishingGeneral abrasive dispersions

    The selection of electronic/EL grade over ready-to-use colloidal silica slurry is often logistics-driven, but powder dispersion must be treated as a process step. Colloidal silica slurry is already discrete and electrostatically stabilized; the powder requires deagglomeration, pH adjustment, filtration, and aging before use. However, the powder can be shipped without water, stored for 24 months in unopened containers, and adjusted to different solids concentrations for different CMP stages. Ready-to-use slurries are subject to settling, microbial growth, and freezing constraints during transport and inventory.

    In sapphire LED substrate polishing, the alkaline silica dispersion is used at pH 10.5–12.0 with polishing temperature maintained at 50–60 °C on a rigid polyurethane pad. Material removal rate is strongly dependent on crystal orientation; C-plane sapphire typically removes 1.0–2.5 µm/h under 400–600 gf/cm² downforce and 70–90 rpm platen speed. The electronic/EL grade reduces sub-surface damage relative to harder alumina abrasives because silica particle hardness is lower than sapphire but remains sufficient for alkaline oxide removal. The dominant failure mode is slurry glazing when pad pores fill with silica and large particles; in situ conditioning and slurry flow above 150 mL/min are required to prevent pad loading.

    Why is predispersion with high-shear mixing necessary before point-of-use blending?

    Dry nano silica powder contains agglomerates formed during drying and packaging. These agglomerates may range from 5 µm to 50 µm as received and do not spontaneously return to primary particles under low-speed impellers. High-shear predispersion is required to reduce the coarse tail before the slurry enters the CMP tool. A typical point-of-use procedure wets the powder into high-purity water at 5–10 wt% under a rotor-stator mixer with tip speed of 15–25 m/s for 30 min. Laboratory batches may then be sonicated at 20 kHz and 500 W for 15 min to bring the D90 below 180 nm.

    The order of pH adjustment is important. If the full KOH charge is added before wetting, localized high-pH zones accelerate silica dissolution and create sodium-rich gel particles that are difficult to filter. If pH is raised after dispersion to 9.5–10.5, the surface charge develops uniformly and the zeta potential stabilizes between −30 mV and −50 mV under ISO 13099-1:2012. The slurry should be kept below 35 °C during mixing; shear heating above 45 °C at high solids can increase viscosity and reduce filter life.

    Filtration of the dispersed slurry through a 0.5 µm depth filter followed by a 0.2 µm membrane reduces the large-particle count from several thousand particles per milliliter to below 100 particles/mL. Membrane filtration above 12 wt% solids may cause rapid fouling; it is preferable to filter at 5–10 wt% and then adjust to final solids rather than filtering the concentrated slurry. The dispersion is incompatible with cationic polyelectrolytes and high concentrations of multivalent metal salts, which compress the electrical double layer and reduce zeta potential below −20 mV, causing flocculation even when bulk pH is within specification.

    The powder is hygroscopic, and exposure to relative humidity above 60% for more than 8 h may raise moisture content above the 2.0 wt% release limit and create hard agglomerates that cannot be fully dispersed under standard point-of-use shear. If moisture uptake occurs, the powder should be re-dried at 120 °C for 2 h under dry nitrogen or vacuum before use. Storage should be in sealed HDPE or 316L stainless steel containers at 5–30 °C; carbon steel and uncoated aluminum equipment must be avoided because iron and aluminum contamination degrade electronic-grade purity. The product is a synthetic amorphous silica; handling should use local exhaust ventilation and appropriate respiratory protection when dust formation exceeds the applicable national occupational exposure limit for respirable amorphous silica. The operational boundary is that this powder is intended for high-purity aqueous dispersion systems in controlled environments, not for dry blasting or direct dry polishing.

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