| HS Code | 563638 |
| Chemical Formula | Al2O3 |
| Purity Percent | ≥99.99 (Electronic/EL Grade) |
| Crystal Phase | alpha-alumina (corundum) |
| Particle Size Distribution | D50 0.3 µm; narrow controlled distribution |
| Particle Morphology | polyhedral/equiaxed |
| Specific Surface Area M2 Per G | 8-12 (BET) |
| True Density G Per Cm3 | 3.95-4.0 |
| Ph 5wt Percent Water Dispersion | 8-9 |
| Water Solubility | insoluble |
As an accredited CMP Abrasive Powder Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CMP Abrasive Powder, Electronic/EL Grade, packaged in sealed polyethylene bags inside fiber drums, 1 kg net weight per container. |
| Container Loading (20′ FCL) | CMP Abrasive Powder (Electronic/EL Grade) shipped as 20' FCL in sealed containers, ensuring contamination-free, safe transport. |
| Shipping | CMP Abrasive Powder (Electronic/EL Grade) should be shipped in sealed, moisture-resistant containers to preserve purity and particle consistency. It is not typically regulated as hazardous under DOT/IMDG when dry; however, packing must prevent dust release. Keep away from moisture, contamination, and static-prone environments during transit. |
| Storage | Store in a sealed, clean container in a cool, dry, well-ventilated area. Protect from moisture, dust, and direct sunlight. Keep away from acids, alkalis, and reactive chemicals. Avoid prolonged exposure to high temperatures. Use dedicated clean utensils to prevent contamination. Follow manufacturer’s shelf-life and handling guidelines for electronic-grade purity. |
| Shelf Life | Shelf life is 12 months from manufacture date when stored sealed in a cool, dry place. |
In shallow trench isolation modules operating below the 45 nm node, oxide planarization with electronic/EL grade ceria-based CMP abrasive powder exposes a narrow process corridor between acceptable silicon dioxide removal rate and silicon nitride stop-layer loss. High-density plasma oxide fill is deposited over a silicon nitride liner at thicknesses between 300 nm and 700 nm, and the subsequent CMP step must clear overburden while leaving the nitride intact for later wet strip. Production-scale polishers configured with 300 mm four-zone membrane carrier heads run platen speeds of 63–93 rpm, downforce of 1.5–3.0 psi, and slurry flow rates of 150–250 mL/min. Motor-current endpoint detection is used, and the over-polish budget is held at 10–15% relative to blanket wafer endpoint time. Beyond that window, nitride corner erosion and trench oxide dishing exceed 15 nm, altering transistor strain and leakage in the completed device.
The final slurry typically contains ceria at 0.5–2.0 wt%, polyacrylic acid dispersant at 0.05–0.3 wt%, and acetic acid to maintain pH at 4.0–4.8. Primary ceria particles are in the range of 20–80 nm, with a volume-median diameter of 50–65 nm and a D90 below 120 nm. At these conditions, blanket PECVD silicon dioxide removal reaches 2200–3500 Å/min, while silicon nitride removal remains below 80 Å/min under the same downforce. The selectivity ratio therefore falls between 30:1 and 45:1, which is necessary to stop on the nitride layer without consuming the active area. Dispersion equipment must deliver rotor tip speeds above 20 m/s; if dispersant adsorption is not completed before the pH drops below 4.0, zeta potential falls below 30 mV, producing aggregates that raise microscratch density above 0.05 defects/cm² on blanket oxide monitors. Ammonium hydroxide is excluded from this formulation because pH above 5.5 reduces the selectivity ratio below 10:1, leading to nitride loss greater than 20 Å/min on blanket films.
Slurry blending and filtration are performed in ISO 14644-1:2015 Class 3 cleanrooms. Particle size distribution is verified by ISO 13320:2020 laser diffraction after high-shear dilution, while nano-scale aggregation is checked with ASTM E2490-08. Trace metal reporting uses ICP-MS with detection limits of 0.1 ppb for iron and 0.05 ppb for sodium. REACH Regulation (EC) No 1907/2006 Article 33 applies to components present at mass fraction above 0.1%. Powder storage is maintained below 60% relative humidity; exposure to higher humidity produces caking that cannot be fully reversed by mechanical milling without shifting the D50 by more than 5%.
Finished wafers proceed to gate stack formation and are integrated into logic and DRAM devices with shallow trench isolation pitch below 100 nm. Terminal product types include logic processors, DRAM arrays, and embedded non-volatile memory. The same oxide-selective ceria formulation is also used for inter-layer dielectric planarization, but the nitride selectivity requirement is relaxed, allowing a larger pH window of 4.0–5.5 and reducing endpoint sensitivity.
The bulk copper removal step on patterned interconnects where the dielectric stack includes porous low-k films with k-value ≤ 2.5 uses colloidal silica abrasives of 20–40 nm primary size at 0.5–2.0 wt% loading. The formulation includes glycine at 0.5–1.5 wt%, hydrogen peroxide at 1.0–3.0 wt%, and benzotriazole at 0.01–0.05 wt%, with pH held at 8.5–10.0 using potassium hydroxide. Removal rates on electroplated copper are typically 5000–9000 Å/min at 2.0 psi downforce, while tantalum nitride removal is suppressed to 400–900 Å/min during the bulk step. The subsequent Ta/TaN barrier polish reduces abrasive loading to 0.1–0.5 wt% to limit mechanical erosion of the underlying ultra-low-k dielectric.
The barrier CMP step on a 300 mm platform must maintain a zeta potential more negative than -40 mV to prevent particle agglomeration near the low-k surface. Low-k delamination occurs when the applied shear stress exceeds 1.5 psi on porous films with elastic modulus below 4 GPa; therefore the carrier downforce is reduced from 2.5 psi to 1.2 psi and platen speed from 90 rpm to 60 rpm for barrier clearing. In-line slurry monitoring checks pH drift caused by hydrogen peroxide decomposition; a shift greater than 0.2 pH units indicates that a fresh oxidizer spike or batch dilution is required. Batch-to-batch variation in colloidal silica surface charge has caused an increase from 0.01 defects/cm² to 0.07 defects/cm² on copper lines when the zeta potential moved to -25 mV, demonstrating the need for electrophoretic light scattering release testing. Amine-based additives are not used in this formulation because adsorption on colloidal silica shifts the zeta potential toward the isoelectric point, causing particle aggregation and higher copper defect density.
Slurry purity is controlled under ISO 14644-1:2015 Class 3 conditions; liquid particle counters calibrated to ISO 21501-2:2007 limit particles at ≥0.2 µm to less than 100 particles/mL. Sodium and potassium are specified below 0.5 ppm, and total transition metals below 1 ppm by ICP-MS. The formulation is registered under REACH (EC) No 1907/2006, and no substance is present above Annex XVII restriction triggers under the defined use conditions. RoHS 2011/65/EU Annex II applies to the finished electronic assembly rather than to the front-end polishing chemistry.
Post-CMP brush cleaning uses 0.5–1.0% ammonium hydroxide and 0.3–0.5% hydrogen peroxide in deionized water to remove copper-organic residues before dielectric cap deposition. Terminal product types are logic processors, graphics processors, and high-bandwidth memory modules with copper/low-k interconnects at pitches below 40 nm. Published data for specific barrier slurry performance on ultra-low-k dielectrics with k < 2.2 is limited; a blanket wafer split-lot should quantify defect density and dielectric loss before committing a production run.
| Downstream application | Abrasive type | Typical addition ratio | Operating pH | Representative removal rate | Primary standard |
|---|---|---|---|---|---|
| STI/ILD oxide planarization | ceria | 0.5–2.0 wt% | 4.0–4.8 | 2200–3500 Å/min | ISO 13320:2020 |
| Copper/low-k damascene | colloidal silica | 0.5–2.0 wt% bulk; 0.1–0.5 wt% barrier | 8.5–10.0 | 5000–9000 Å/min copper | ISO 21501-2:2007 |
| 4H-SiC substrate | monocrystalline diamond | 1.0–4.0 wt% | 10.5–11.5 | 1–3 µm/hr | ASTM E2490-08 |
| Electroless nickel-polished aluminum disks | alumina | 0.05–0.8 wt% | 2.0–3.0 | 0.1–0.3 µm/min | ISO 13320:2020 |
| Sapphire LED substrate | colloidal silica | 10–20 wt% | 10.5–11.5 | 0.5–1.5 µm/hr | ISO 22412:2017 |
| Display glass edge treatment | ceria | 2–6 wt% | 10.0–11.0 | 0.5–1.5 µm/min | RoHS 2011/65/EU Annex II |
Because single-crystal 4H-SiC wafers exhibit a basal plane microhardness of 28–32 GPa, material removal rates plateau below 200–400 nm/hr when conventional colloidal silica abrasives are used at neutral pH, even at downforces above 6 psi. Production lines therefore use monocrystalline diamond abrasives with an engineered bimodal distribution to reach 1–3 µm/hr without generating deep scratches. A typical formulation combines 100–150 nm diamond primary particles at 70–80% of total abrasive mass with 20–40 nm secondary particles at 20–30%, dispersed to a final loading of 1.0–4.0 wt% in an aqueous medium containing 0.5–1.5 wt% hydrogen peroxide or 0.1–0.3 wt% potassium permanganate at pH 10.5–11.5. The small-particle fraction fills interstitial gaps and reduces peak contact pressure, while the large-particle fraction maintains mechanical indentation depth sufficient for C-face or Si-face material removal.
Processing is carried out on rigid polyurethane pads with 60–65 Shore D hardness, platen speed of 60–80 rpm, downforce of 3.0–6.0 psi, and slurry flow of 100–200 mL/min. Continuous in situ pad conditioning with a diamond disk at 0.5–1.0 psi prevents pad glazing; without conditioning, removal rate falls by 20–30% within the first 50 wafers. Wafer surface temperature is monitored by infrared pyrometry and maintained below 30 °C to prevent oxidizer decomposition and particle dry-out at the pad edge. Post-CMP cleaning uses SC-1 solution at 65–70 °C followed by dilute hydrofluoric acid to remove silica-based contamination and subsurface damaged material.
Particle size distribution is verified against ISO 13320:2020 and ASTM E2490-08. Scratch density is measured by unpatterned wafer inspection tools operating at 60 nm equivalent sensitivity; qualification requires fewer than 0.02 scratches/cm² after 4-inch or 6-inch wafer polishing. Cleanroom classification during final polishing is ISO 14644-1:2015 Class 4. The abrasive powder is subject to REACH (EC) No 1907/2006 Annex XVII considerations for fine particulate if supplied as an unbound powder, and safety data sheets follow CLP (EC) No 1272/2008.
Finished substrates are used for epitaxial growth of silicon carbide metal-oxide-semiconductor field-effect transistors and Schottky barrier diodes in 650 V, 1200 V, and 1700 V power modules, as well as for GaN-on-SiC RF devices in 5G base station power amplifiers. Published data for exact scratch density on C-face 4H-SiC under 3 psi conditions is limited; each slurry batch must be qualified by atomic force microscopy on a 10 µm × 10 µm scan area with RMS roughness below 0.3 nm and by cross-sectional transmission electron microscopy for subsurface damage depth below 5 nm.
The electroless nickel-phosphorus plating on aluminum disk substrates produces an amorphous surface layer 10–12 µm thick, which must be polished to remove plating nodules and waviness without cutting through to the aluminum base. High-purity alumina abrasive at 0.05–0.8 wt% loading in a slurry with pH 2.0–3.0 adjusted by nitric acid or citric acid produces a NiP removal rate of 0.1–0.3 µm/min and suppresses micro-waviness. Hydrogen peroxide at 0.5–1.0 wt% is included to maintain a passive oxide film and reduce nickel dissolution pits. Aluminum substrates are not exposed until the NiP layer has been uniformly planarized, preventing galvanic corrosion between the aluminum and the nickel-phosphorus alloy.
Polishing tools use multi-head rotary configurations with polyurethane pads and continuous diamond conditioning. Disk rotation is set to 30–60 rpm, pad rotation to 25–50 rpm, and applied pressure between 0.3 and 1.0 psi. The slurry is recirculated through 0.5 µm filtration with pH and particle size monitored every 30 min; oversized particles above 0.5 µm are controlled below 1000 particles/mL to avoid scratches with a depth greater than 1 nm. Chloride contamination above 10 ppm in the slurry water increases pitting density on the finished NiP surface; therefore water purification must achieve 18.2 MΩ·cm resistivity and chloride below 5 ppb.
Cleanroom classification for substrate polishing is ISO 14644-1:2015 Class 5, and particle size distribution is tested per ISO 13320:2020. Surface roughness control uses phase-shifting interferometry with a 0.5 mm × 0.5 mm measurement area, requiring Ra below 0.1 nm and waviness amplitude below 0.5 nm over a 2 mm scan length. REACH (EC) No 1907/2006 and RoHS 2011/65/EU Annex II apply to the final hard disk assembly rather than to the polishing slurry, but abrasive powder suppliers provide trace metal certificates under ISO 9001:2015.
Finished substrates are sputtered with cobalt-based perpendicular media and diamond-like carbon overcoats, then assembled into 2.5-inch and 3.5-inch hard disk drives used in data center and nearline storage. Batch-to-batch alumina pH drift above 0.1 units has been observed when nitric acid is not pre-diluted, causing removal rate shifts of 8–12% on production lines; therefore acid dosing is performed by closed-loop conductivity control.
On production-scale sapphire wafer lines targeting 2-inch to 6-inch C-plane wafers for gallium nitride epitaxy, post-lapping CMP with high-purity colloidal silica is operated at 10–20 wt% solids and pH 10.5–11.5. The slurry is heated to 45–55 °C to accelerate chemical attack on the sapphire basal plane, achieving a removal rate of 0.5–1.5 µm/hr with a surface roughness Ra of 0.05–0.10 nm over a 10 µm × 10 µm atomic force microscopy scan. Potassium hydroxide or sodium hydroxide at 0.5–2.0 wt% serves as the pH adjuster and etchant, while a polycarboxylate dispersant at 0.01–0.05 wt% maintains particle suspension stability under elevated temperature.
Production polishers use polyurethane pads with 60–65 Shore D hardness, platen speed of 50–80 rpm, downforce of 3.0–6.0 psi, and slurry flow rate of 100–200 mL/min. Diamond pad conditioning is performed ex situ for 5–10 min after each batch of 25 wafers; in situ conditioning is avoided because additional diamond debris can generate deep scratches beyond 1 µm that are not removed by short subsequent polishing. The process terminates when laser confocal inspection shows no scratches larger than 0.5 µm and total thickness variation below 2 µm across a 6-inch wafer. Sodium accumulation on the pad after 25-wafer batches has been observed as haze on the wafer edge; a deionized water rinse step at 50–60 °C for 3 min between batches reduces the defect count by roughly one order.
Slurry dilution and dispensing occur in ISO 14644-1:2015 Class 4 cleanroom; particle size distribution is characterized by ISO 22412:2017 dynamic light scattering with a polydispersity index below 0.05. Sodium and potassium levels are monitored because residual ions migrate into the subsequent metal-organic chemical vapor deposition reactor; specifications are < 1 ppm total alkali metals, and iron is held below 0.5 ppm by ICP-MS. REACH (EC) No 1907/2006 Article 33 and CLP (EC) No 1272/2008 apply to the commercial slurry. Published data for pad break-in effects on wafer edge roughness is limited, so production facilities use dummy sapphire wafers to condition the pad before critical lots.
Finished wafers enter hydride vapor phase epitaxy or metal-organic chemical vapor deposition for gallium nitride LED structures. Terminal product types are near-ultraviolet, blue, and green LED chips used in general lighting, automotive forward lighting, and display backlight units.
TFT-LCD cover glass and touch sensor substrates in thicknesses from 0.2 mm to 1.1 mm are edge-ground and polished with ceria powder blended at 2–6 wt% in deionized water, pH adjusted to 10.0–11.0 with potassium hydroxide, and stabilized with a nonionic dispersant at 0.01–0.10 wt% on automated brush/pad edge treatment lines operating under ISO 14644-1:2015 Class 8 cleanroom conditions; the final cover glass and touch sensor substrates are compliant with RoHS 2011/65/EU Annex II and REACH (EC) No 1907/2006, with a chamfer surface roughness Ra below 20 nm and chipping depth below 50 µm.
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Chemical mechanical planarization abrasive powder designated as Electronic/EL Grade is supplied as a dry, high-purity abrasive feedstock for custom slurry formulation in semiconductor wafer processing. The “EL” designation denotes electronic-grade controls rather than a fixed chemical composition; the powder may be specified as high-purity silica, colloidal silica precursor, or high-purity alumina depending on the supplier product family. Because product model codes remain supplier-specific, an EL-grade lot is typically identified by a base-chemistry code followed by a primary-particle-size class and a surface-treatment suffix, such as SiO2-EL-50-K or Al2O3-EL-120-N; no universal numbering convention is available across manufacturers. Certificate-of-analysis data usually include ignition loss, specific surface area, D50, D90, D99, total metal impurities by inductively coupled plasma mass spectrometry, and large-particle count after high-shear dispersion. The powder is used at the point of slurry blending to control material removal rate, wafer-level defectivity, and post-CMP cleanability on dielectric, copper, tungsten, and shallow-trench-isolation films.
A certificate of analysis for an EL-grade lot should be read against the intended slurry formulation rather than as a generic purity statement. Production-scale blending skids commonly require lot-to-lot D50 variation within ±5% of the approved mean because a shift of 10 nm in D50 can alter material removal rate by 5% to 10% on some oxide films. However, the quantitative relationship between D50 and removal rate is pad- and slurry-chemistry dependent; published data for this specific configuration are limited, and a single universal conversion factor does not exist. Storage life for unopened powder is typically 12 months from production date when kept at 15 °C to 25 °C and below 40% RH. Exposure above 60% RH requires pre-drying at 120 °C for 2 h before use to prevent feed-hopper caking and inconsistent solids dosing.
General-purpose lapping or metallographic abrasives are commonly supplied to wider size distributions and higher metallic impurity ceilings because their end use is dimensional material removal, not device-grade planarization. Electronic/EL Grade is controlled at the dry-powder stage for upper-tail particles, total metal contamination, and alpha-emitting radionuclides where specified. The distinction is not solely chemical: a high-purity alumina general abrasive may share a base chemistry with an EL-grade alumina powder but still fail electronic-grade lot acceptance because the particle-size distribution has a long coarse tail. The acceptance ranges in the table below are representative supplier lot-release values; a valid comparison requires certificate-of-analysis data from the same test methods.
| Parameter | Electronic/EL Grade | General-purpose abrasive | Test method |
|---|---|---|---|
| Primary particle D50 | 20 nm to 150 nm | 0.3 µm to 3 µm | ISO 22412:2017 |
| Size-distribution span | ≤ 0.8 | > 1.2 | ISO 22412:2017 |
| Large-particle count, ≥ 0.5 µm | < 2,500 particles/mL in 5 wt% dispersion | > 50,000 particles/mL | ISO 21501-2:2019 |
| Total trace metals | < 10 ppm total; alkali/alkaline earth < 0.5 ppm | < 500 ppm total | SEMI C1-aligned ICP-MS |
| Alpha-particle emission | ≤ 0.01 counts/cm²·h where specified | not controlled | low-background gas-flow proportional counting |
The most operationally significant difference is not the mean particle size but the upper tail. A general-purpose powder with the same D50 as an EL-grade powder may contain a small fraction of coarse particles large enough to create microscratches on copper or low-k surfaces; this fraction is invisible to a simple D50 measurement and must be controlled by large-particle counting.
Dry EL-grade powders are rarely introduced directly into the CMP tool; they are first converted into a slurry concentrate in a dedicated blend skid. Deionized water with resistivity above 18 MΩ·cm at 25 °C and total organic carbon below 20 ppb is used for make-down; untreated municipal water is incompatible because hardness and colloidal contaminants can destabilize the dispersion. A production-scale rotor-stator mixer operating at 16 m/s to 22 m/s tip speed for 20 min to 30 min is typically required to wet the powder and reduce agglomerates. High-energy mixing beyond 30 min can erode stainless-steel contact surfaces and introduce Cr, Ni, and Fe contamination. Where lower large-particle counts are needed, the slurry is recirculated through an in-line high-pressure homogenizer at 1,000 bar to 1,500 bar with a ceramic interaction chamber, followed by a 0.5 µm or 0.2 µm polyethersulfone membrane filtration step.
Particle-size distribution of the diluted slurry is measured by dynamic light scattering according to ISO 22412:2017; laser diffraction per ISO 13320-1:2020 is less reliable below 100 nm. For a well-dispersed EL-grade silica slurry, the Z-average may be 5 nm to 15 nm larger than the primary-particle D50 due to the hydrated or stabilized surface layer, and the polydispersity index should remain below 0.08. A polydispersity index above 0.20 after high-shear dilution usually indicates incomplete deagglomeration, salt-induced coagulation, or microbial growth. Zeta potential is measured by electrophoretic light scattering according to ISO 13099-2:2012; stable silica-based EL slurries at pH 9 to 10 generally maintain zeta potential more negative than −30 mV.
For alumina-based EL-grade powders, formulation near the isoelectric point pH 8 to 9 can increase slurry viscosity by an order of magnitude and produce shear-thinning behavior; such a slurry typically fails pump and filtration specifications. Maintaining pH at least 1.5 units away from the isoelectric point is therefore recommended. In addition, make-down water temperature should be maintained below 30 °C; elevated temperature accelerates surface hydration and can create gel-like fines that shift the apparent D50 and raise large-particle counts.
Total metal impurities in Electronic/EL Grade powders are typically determined by ICP-MS after closed-vessel microwave acid digestion, using protocols aligned with SEMI C1 guidelines. Individual transition-metal limits for Fe, Cu, Cr, and Ni are generally below 1 ppm; Na and K are commonly held below 0.5 ppm because residual mobile ions degrade gate-oxide integrity and shift threshold voltage. Al and Ca are also controlled because they can form insoluble residues that increase post-CMP defect counts. However, the EL label is not a substitute for lot-level testing: ion contamination can be introduced from packaging, transfer lines, or make-down water. Equipment contact surfaces should be fluoropolymer or electropolished stainless steel; unlined carbon steel and aluminum transfer components are incompatible due to Fe and Al pickup above 1 ppm.
For memory and logic devices susceptible to soft errors, alpha-particle emission from process materials must be controlled. Electronic/EL Grade powders intended for ultralow-alpha applications are measured by low-background gas-flow proportional counting and commonly require ≤ 0.01 counts/cm²·h; general-purpose abrasive powders are not measured for alpha flux. Not every EL-grade product is automatically ultralow-alpha, so a specific alpha specification must be placed on the purchase order when required. In addition, the powder should not be combined with amine-based dispersants that can complex transition metals or leave organic residues after oxide polishing; where amine additives are unavoidable, post-CMP cleaning must be re-validated on the target dielectric stack.
Large-particle counts are measured after dilution by single-particle optical sensing according to ISO 21501-2:2019. The acceptance limit is usually stated at ≥ 0.5 µm because particles in this size bin correlate with microscratches on low-k dielectric and copper damascene surfaces. A representative electronic-grade slurry at 5 wt% solids may be required to contain fewer than 2,500 particles/mL at ≥ 0.5 µm after membrane filtration. The corresponding general-purpose abrasive dispersion can exceed 50,000 particles/mL because the coarse tail is not controlled. Large-particle count alone does not guarantee scratch-free polishing: slurry pH, pad condition, downforce, and in-situ conditioning all influence scratch formation.
Lot release criteria for EL-grade powders should be generated on the same dispersion protocol and test method used in production; switching particle-size metrology from dynamic light scattering to centrifugal sedimentation without re-qualification can mask changes in the fine or coarse tail. For oxide polishing on a 300 mm CMP platform at 3 psi downforce and 1.0 mL/min slurry flow, scratch defectivity is commonly evaluated by laser scattering inspection after 60 s polish. Published data for this specific configuration are limited, and defect thresholds vary with pad stack and consumable set. A lot that passes large-particle specification may still produce high scratch counts if the pad dressing schedule or slurry filtration is inadequate.
In copper barrier CMP, EL-grade silica with a D50 of 20 nm to 50 nm is typically formulated at pH 8 to 10 with a corrosion inhibitor and an oxidizer. The fine particle size reduces platen loading and minimizes low-k scratch damage, but removal-rate control depends on the dispersion state and slurry selectivity. For tungsten CMP, silica or alumina EL-grade powders are used in acidic formulations; alumina-based powders can increase removal rate but require strict control of Al contamination during post-CMP cleaning.
Shallow-trench-isolation CMP slurries may use ceria or silica EL grades to achieve high oxide-to-nitride selectivity, with the powder’s large-particle tail directly influencing nitride erosion and oxide dishing. In all cases, the powder must be qualified on the target polisher and post-clean sequence because no dry-powder specification can fully capture slurry performance.