| HS Code | 999400 |
| Product Name | Ruthenium Metal Polishing Slurry Electronic/EL Grade |
| Abrasive Type | Colloidal Silica |
| Abrasive Particle Size | 30-80 nm |
| Ph | 4.0-6.0 |
| Solids Content | 5-15 wt% |
| Density | 1.01-1.10 g/cm³ |
| Viscosity | 1.5-5.0 cP |
| Ruthenium Removal Rate | 1000-3000 Å/min |
| Selectivity Ru Teos | 20:1 to 50:1 |
| Oxidizer Content | Hydrogen Peroxide or Nitric Acid based |
| Purity | EL Grade, <1 ppm metallic impurities |
| Particle Count | <100 particles/mL (≥0.5 µm) |
| Shelf Life | 6-12 months |
| Storage Temperature | 5-25 °C |
As an accredited Ruthenium Metal Polishing Slurry Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ruthenium Metal Polishing Slurry, Electronic/EL Grade, supplied as 1 gallon (3.78 L) in a sealed HDPE bottle with tamper-evident packaging and label. |
| Container Loading (20′ FCL) | 20′ FCL loading: secure ruthenium polishing slurry in sealed drums/pails on pallets, properly labeled, braced, and ventilated as per chemical shipping regulations. |
| Shipping | This electronic-grade ruthenium polishing slurry ships in sealed, corrosion-resistant containers to maintain purity and stability. Ground freight only within continental regions; expedited delivery available upon request. Not classified as hazardous material for standard transport, but proper labeling and temperature-controlled handling are recommended to preserve performance. |
| Storage | Store in a tightly sealed original container in a cool, dry, well-ventilated area away from direct sunlight and incompatible materials. Maintain temperatures between 5–35°C; do not allow to freeze. Keep segregated from acids, oxidizers, and reducing agents. Use appropriate PPE when handling. Follow manufacturer’s shelf-life guidelines to ensure product stability. |
| Shelf Life | Shelf life is typically 6 months from manufacture date when stored sealed at recommended room temperature. Avoid freezing, agitation, or contamination. |
Ruthenium liners are integrated into copper dual damascene flows at linewidths where conventional TaN/Ta barrier resistivity consumes significant cross-sectional copper volume. Atomic layer deposition produces a Ru layer of 3–6 nm on low‑k dielectrics after barrier metal deposition. The ruthenium slurry is applied after bulk copper removal and must clear the Ru films while stopping on carbon-doped oxide or porous low‑k dielectrics. On 300 mm rotary CMP tools such as the Applied Materials Reflexion LK or Ebara FREX 300, typical process parameters are downforce 1.2–2.5 psi, platen speed 70–100 rpm, head speed 60–90 rpm, and slurry flow 150–300 mL/min. Pad choice is often a hard polyurethane pad with in-situ diamond disk conditioning to maintain surface texture. The transition from copper to ruthenium to low‑k generates a distinct motor current signature because the coefficient of friction changes at each interface. Closed-loop endpoint algorithms using Fourier transform analysis of motor current are implemented to stop the polish before excessive dielectric erosion occurs.
The slurry system uses colloidal silica with a mean particle size 30–60 nm measured by dynamic light scattering per ISO 22412:2017. The oxidizer package is usually periodate-based rather than hydrogen peroxide because periodate drives ruthenium oxidation at a controlled rate while limiting RuO4 volatilization at alkaline pH. The pH is buffered in the range 8–10 with KOH or with an organic alkaline buffer; this range shifts the ruthenium surface to a mixed RuO2/RuO4²⁻ state and reduces the violet RuO4 vapor pressure that appears in acidic formulations below pH 3. Removal rate and selectivity to low‑k are monitored with patterned wafer testing; final dielectric erosion is typically held below 2–3 nm per barrier clear. Post-cleaning uses dilute organic acid or TMAH-free formulations to remove silica and metal residues without increasing porous low‑k k-value shift. Slurry filtration through a 0.1 µm membrane is mandatory before dispense because oversized particles generate micro-scratches that compromise line yield at sub‑7 nm nodes.
The planarization of ruthenium hard masks on DRAM capacitor modules is constrained by the need to preserve tight capacitor height and avoid dishing across high-density cylinder arrays. Ruthenium hard mask overlayers are deposited over dielectric or TiN/high‑k stacks, and CMP removes the hard mask after electrode etchback. The slurry requires high Ru removal rate but low removal of the sublayer, typically TiN or silicon dioxide, to prevent capacitor height collapse. Process conditions on 300 mm systems use low downforce 1.0–2.0 psi to limit delamination at the Ru/dielectric interface; platen speed is maintained between 60–90 rpm and the head is operated in a floating mode to manage wafer curvature generated by thick memory stack films. Endpoint detection uses motor current or eddy current signatures because the Ru hard mask layer has a distinct frictional response.
Formulation design for this segment diverges from logic slurries because the Ru surface area on patterned capacitor wafers is highly localized and the pattern density varies across the die. Ceria abrasives or mixed silica-ceria slurries are used to raise Ru removal rate without aggressive pad embossing. The oxidizer concentration is adjusted to give a Ru removal rate in the 30–70 nm/min range on blanket films, with a removal rate ratio of Ru:TiN above 5:1 in typical process qualification. Selectivity to silicon dioxide is tested by measuring oxide erosion on 100 µm line/space patterns with an atomic force profiler; oxide loss is commonly specified below 3 nm after endpoint. Batch-to-batch variation in abrasive aggregate size is controlled by large-particle counting and zeta potential measurement; slurry with aggregate counts above 100 counts/mL at ≥0.5 µm is rejected before dispense. The terminal capacitor device requires uniform electrode height because uneven planarization shifts capacitance distribution and degrades refresh time in high-density DRAM architectures.
In copper interconnect reliability builds, ruthenium capping layers of 2–5 nm are selectively deposited onto Cu lines to suppress electromigration and improve adhesion to the surrounding dielectric. A low-pressure touch CMP operation removes the ruthenium overburden from the adjacent dielectric while preserving the Ru cap over Cu. This operation uses a high-selectivity slurry that oxidizes ruthenium rapidly but passivates Cu through an inhibitor system. The touch CMP step is run at downforce 0.5–1.2 psi on soft or hybrid pads to avoid increasing line resistance by thinning the Cu cap. The dielectric loss limit is tighter than in standard barrier CMP; post-touch oxide erosion below 1.5 nm is required in many 300 mm process specifications.
Formulations for Ru cap touch polishing often replace standard silica with low-abrasive or abrasive-free oxidizer solutions to minimize scratches on Cu and low‑k surfaces. The oxidizer is typically an aqueous solution of periodate or persulfate at acidic-to-neutral pH, combined with a Cu corrosion inhibitor such as benzotriazole at 0.01–0.1 wt%. The endpoint is determined by monitoring Cu or Ru thickness through eddy current measurements on a post-CMP metrology stand. Slurry filtration through a 0.1 µm membrane is mandatory because large particles induce line micro-scratches in low‑k areas. The material is dispensed through an integrated slurry delivery system with low-shear diaphragm pumps and point-of-use ultrasonication to break down soft agglomerates without fracturing abrasive particles. In high-volume production, the touch polish is sequenced immediately after the main barrier CMP step to prevent air exposure of the copper surface from promoting corrosion under residual slurry films.
Because ruthenium possesses a more noble electrochemical potential than copper, an aqueous CMP environment can form a galvanic couple at the Cu/Ru interface when both metals are exposed during barrier clearing. This couple drives enhanced Cu dissolution or pitting if the slurry lacks an effective copper inhibitor. Formulations for Ru barrier clearing therefore incorporate azole derivatives, typically benzotriazole or tolyltriazole, at concentrations between 0.005 and 0.1 wt%, to form a Cu-benzotriazole film that reduces the corrosion current density. Electrochemical measurements using rotating disc electrodes in pH 8–10 periodate systems show that the Cu static etch rate must be held below 1 nm/min and the Ru static etch rate below 2 nm/min to maintain final metal line integrity. Patterned wafer open-circuit potential differences are controlled by reducing oxidizer concentration after endpoint and adding a conductivity-adjusting salt to keep slurry conductivity below 200 µS/cm.
Pitting on ruthenium films after CMP is often caused by local accumulation of RuO4 or by residual ceria or silica particles adhering to the surface. A post-CMP clean sequence with dilute oxalic acid or citric acid at pH 2–4 is applied on polishing platforms fitted with brush stations. Brush cleaning uses PVA brushes and a rinse of ultra-pure water with CO2 injection to prevent particle redeposition. The cleaned wafers are then dried in an isopropyl alcohol vapor dryer. Defect metrology on KLA Surfscan SP2 or SP3 instruments at capture size 0.16 µm typically monitors post-barrier CMP defect density; a release limit below 50 defects per wafer is used in many advanced logic flows. The ruthenium slurry itself is specified with anion tolerance because residual chloride or sulfate aggravates pitting and must be controlled below 10 ppm by ion chromatography per ISO 10304-1:2009.
Embedded MRAM flows that integrate perpendicular magnetic tunnel junction stacks introduce a ruthenium CMP challenge in which the Ru layer may act as a spacer or hard mask and must be polished without damaging thin MgO tunnel barriers beneath. The Ru film thickness in pMTJ hard mask stacks is typically in the 5–30 nm range, and the CMP process is used to planarize the top Ru layer before etch or to remove a sacrificial Ru mask after patterning. Because the underlying magnetic stack is sensitive to mechanical stress and metal ion diffusion, the slurry must be formulated with ultralow trace metal contamination and low downforce. Polishing parameters are limited to 0.5–1.5 psi downforce and platen speeds of 40–70 rpm, often on a soft pad to reduce shear stress.
The terminal devices require ruthenium remaining only on defined magnetic tunnel junction pillars; residual Ru metal ion contamination above 10¹⁰ atoms/cm² on the surrounding dielectric can shift tunneling magnetoresistance and degrade magnetic anisotropy. Slurry suppliers therefore control transition metal impurities by ICP-MS using an acid-hydrolyzed digest and a cleanroom bottling environment. The abrasive concentration is reduced to minimize scratching of the MgO interface; formulations may use colloidal silica at 0.5–2 wt% solids loading with a mean particle size below 40 nm. Process qualification includes patterned MRAM wafer tests measuring shorting between top and bottom electrodes and normalized TMR retention after annealing at 300 °C for 60 min. Batch release requires a particle size distribution uniformity where the D90/D50 ratio is less than 1.5 by ISO 22412:2017 dynamic light scattering.
EL-grade ruthenium metal polishing slurry for 300 mm fabrication facilities is released against a comprehensive impurity budget that aligns with front-end-of-line contamination requirements. The slurry is packaged in fluoropolymer-lined drums and dispensed through a filtration loop that maintains particle size stability over a 30-day shelf life. The release table below lists the main electronic-grade control points and the corresponding metrology used in high-volume CMP lines.
| Control point | Test method / condition | EL-grade control band |
|---|---|---|
| Mean particle size D50 | ISO 22412:2017 dynamic light scattering at 25 °C | 30–60 nm |
| Large particle counts ≥0.5 µm | Single-particle optical sensing after 10× dilution | <100 counts/mL |
| Total trace metal cations excluding Ru | ICP-MS after closed-vessel acid digestion | <10 ppm for mobile ions; <1 ppm for Cu and Fe |
| pH | ISO 10523:2008 pH measurement | Lot-specific target ±0.2 |
| Static etch rate on blanket Ru | Polished coupon immersion test | <2 nm/min |
The dispense system uses low-shear diaphragm pumps and point-of-use 0.1 µm filters to prevent aggregate introduction. Slurry batches are qualified on a monitor wafer before lot release; the monitor wafer removal rate must fall within a defined control range, commonly centered at 30–70 nm/min for blanket Ru films. Viscosity is held between 1.0 and 3.0 mPa·s at 25 °C to ensure stable pad film thickness and uniform wafer-scale removal. Cleanroom bottling is conducted under ISO 14644-1 Class 5 conditions to limit airborne particle contamination. The terminal product in all described segments is a planarized 300 mm wafer with ruthenium remaining only in designed features, ready for post-CMP clean and subsequent dielectric or electrode deposition.
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Ruthenium Metal Polishing Slurry Electronic/EL Grade is a colloidal silica-based chemical-mechanical planarization dispersion formulated for selective removal of chemical vapor deposited or atomic layer deposited ruthenium barrier, liner, and via-fill films. The product model RUT-EL-75/PER comprises 5 wt% colloidal silica with a nominal median particle diameter of 75 nm and a periodate-based oxidizer package. The EL designation is assigned when lot release data confirm total transition metal impurities below 100 μg/L, chloride and nitrate below 500 μg/L, and large particle count for particles ≥ 0.15 μm below 200 particles/mL by single-particle optical sensing per ISO 21501-2:2019. The dispersion has a pH of 6.2–7.0 at 25 °C measured by ASTM E70-19 and a dynamic viscosity of 1.8–2.6 mPa·s at 100 s⁻¹ per ASTM D2196-20. The zeta potential in the native pH range is −28 to −34 mV per ISO 13099-1:2024, providing electrostatic stabilization against agglomeration. The formulation targets a ruthenium removal rate of 45–80 nm/min on 300 mm rotary CMP platforms at 2.0 psi downforce, 90 rpm platen speed, and slurry flow rate of 200 mL/min, while the copper removal rate under those conditions is held below 5 nm/min.
On production-scale 300 mm barrier polishing systems with integrated wafer-level endpoint, the slurry is dispensed through point-of-use filtration with 0.1 μm rated polypropylene depth filters and a bellows pump. Batch-to-batch oxidizer variation shifts ruthenium removal rate by approximately 10–15% if the slurry is held at 25 °C beyond 72 h after wetting. The material is therefore filled in single-use containers under ISO Class 4 conditions per ISO 14644-1:2015 and assigned a shelf life of 6 months at 4–20 °C. Freezing must be avoided; frozen silica slurries undergo irreversible aggregate formation that can increase large particle counts by more than two orders of magnitude. The slurry is incompatible with strong reducing agents and with amine-based post-CMP clean chemistries, which can prematurely reduce the periodate oxidizer and lower Ru removal rate. Transfer should be carried out with pressure-assisted dispensing using a nitrogen headspace below 0.1 MPa, not by direct pouring from a secondary container.
The primary differences are trace metal purity, particle size distribution width, and defect generation after barrier clearing. General-purpose ruthenium slurries may contain total metal impurities in the 1–10 mg/L range, whereas RUT-EL-75/PER is released only when ICP-MS analysis in an ISO/IEC 17025:2017 accredited laboratory shows Na, K, Fe, Ni, Cu, and Cr each below 100 μg/L and total transition metal content below 500 μg/L. Particle size distribution is controlled to a polydispersity index below 0.10 per ISO 22412:2017, compared with 0.15–0.25 for several non-EL silica slurries used in early process development. Inline dark-field inspection after 120 s brush cleaning has shown micro-scratch density below 2.0 scratches/cm² at 0.1 μm pixel resolution for the EL grade, while conventional silica-based ruthenium slurries can exceed 8 scratches/cm² under the same pad and downforce conditions. The oxidizer package maintains a Ru-to-Cu removal selectivity of at least 10:1 and Ru-to-TEOS dielectric selectivity above 8:1 on a 100/70 pad stack. Alumina-based ruthenium polishing dispersions are not recommended for this integration because hard abrasive particles increase low-k erosion and micro-scratch formation; published comparative data for this specific configuration remain limited beyond inline monitor trends.
| Characteristic | RUT-EL-75/PER | Conventional silica-based Ru slurry |
|---|---|---|
| Total transition metal impurities | ≤0.5 mg/L | 1–10 mg/L |
| Polydispersity index | ≤0.10 | 0.15–0.25 |
| Micro-scratch density after brush clean | <2.0 scratches/cm² | >8.0 scratches/cm² |
| Cu removal rate at 2.0 psi, 90 rpm | <5 nm/min | 10–20 nm/min |
| Ru-to-TEOS selectivity | >8:1 | 2:1–5:1 depending on pad |
| Settled solids after 7 days at 20 °C | <0.1 vol% | 0.5–1.0 vol% |
Removal of ruthenium in this system proceeds through electrochemical oxidation of Ru(0) to Ru(II)/Ru(III) surface oxides followed by mechanical abrasion by colloidal silica. The periodate oxidizer maintains a redox potential of approximately +0.8 to +1.0 V versus Ag/AgCl at pH 6.5, which is below the regime of aggressive RuO4 volatilization. Static etch rate of ruthenium in the absence of mechanical activation is less than 0.5 nm/min at 25 °C, indicating chemically assisted abrasion rather than isotropic wet etching. This is critical for barrier clearing endpoints because low static etch suppresses recess in dense line arrays. In situ pad conditioning with a diamond conditioner of 250–350 μm grit size is required to maintain removal rate stability; pad glazing from accumulated ruthenium oxide can reduce removal rate by up to 20% over 50 wafers if conditioning is interrupted. The slurry flow rate is maintained at 180–220 mL/min to avoid depletion of oxidizer at the pad-wafer interface.
The colloidal silica abrasive is specified to provide a combination of mechanical removal and low defectivity. The following lot release specification applies to the RUT-EL-75/PER model.
| Parameter | Limit | Test method |
|---|---|---|
| Median particle diameter (D50) | 70–80 nm | ISO 22412:2017 |
| Polydispersity index | ≤0.10 | ISO 22412:2017 |
| pH at 25 °C | 6.2–7.0 | ASTM E70-19 |
| Dynamic viscosity at 100 s⁻¹ | 1.8–2.6 mPa·s | ASTM D2196-20 |
| Zeta potential | −28 to −34 mV | ISO 13099-1:2024 |
| Large particle count ≥ 0.15 μm | ≤200 particles/mL | ISO 21501-2:2019 |
| Na, K, Fe, Ni, Cu, Cr each | ≤100 μg/L | ICP-MS, ISO/IEC 17025:2017 |
| Total transition metals | ≤500 μg/L | ICP-MS, ISO/IEC 17025:2017 |
| Chloride and nitrate | ≤500 μg/L | Ion chromatography |
The zeta potential is maintained between −28 and −34 mV to balance electrostatic stabilization against the dispersive action of the low-molecular-weight anionic additive. If the zeta potential magnitude drops below 20 mV, the dispersion can undergo shear-induced agglomeration in recirculation loops, raising large particle counts above the 200 particles/mL threshold. The trace metal budget is not solely a purity specification; transition metals such as Fe and Cu at part-per-million levels can act as Fenton-type or electrochemical catalysts that destabilize the oxidizer package and increase static etch of copper. Lot release therefore records the individual and total concentrations by ICP-MS with reporting limits of 0.1 μg/L for Na and K and 0.05 μg/L for Cr and Ni.
In copper dual-damascene integration, the slurry is applied after copper bulk removal and before dielectric barrier capping. The Ru liner thickness is typically 2–5 nm at the 7 nm and 5 nm technology nodes; endpoint is based on motor current shift and optical reflectance. A 30–60% overpolish after endpoint is used to clear ruthenium residues from dense line and via arrays, while the low-k dielectric loss budget is held below 3 nm by adjusting downforce within the 1.8–2.3 psi window. The slurry is also used in through-silicon via reveal processes in which Ru seed layers are exposed after backside grinding; there, the removal rate on ruthenium is intentionally reduced to 30–45 nm/min by lowering platen speed to 60 rpm to reduce edge effect. In both applications, post-polish cleaning uses dilute organic acid or citric acid-based solutions; the slurry must be rinsed from the pad before pad dressing to prevent redeposition of Ru oxide onto the collar and retainer ring.
Central delivery of RUT-EL-75/PER is acceptable only with continuous low-shear recirculation below 300 s⁻¹ and a maximum loop pressure of 0.3 MPa. Residence time in the loop must not exceed 48 h at 20 °C; periodate decomposition under recirculation reduces oxidizer activity and can lower Ru removal rate below 30 nm/min. Point-of-use filtration with 0.1 μm rated polypropylene filters is mandatory, and filters must be flushed with ultrapure water before slurry introduction to remove metallic extractables. Ultrasonic flow sensors have been observed to generate micro-bubbles that increase defect counts after pad contact; mass flow controllers with sapphire or PTFE wetted parts are preferred in the dispense line. The slurry must not be mixed with copper bulk CMP residues in shared effluent without pH neutralization to 7–9 and oxidation-reduction potential quenching, because residual periodate can continue etching copper at the bevel and backside if carryover occurs.
The product is supplied with certification of analysis including lot-specific pH, viscosity, D50, and trace metal data. At relative humidity above 60%, the container should be opened only in a nitrogen-purged cabinet to avoid carbon dioxide uptake that can drift pH and shift zeta potential. Re-circulation pumps should use ethylene propylene diene monomer or perfluoroalkoxy wetted parts; silicone tubing is not accepted because it releases siloxanes that can alter particle surface charge. For pad stacks, a 100/70 polyurethane pad configuration with sub-pad depth 0.8–1.2 mm is standard; hard felt pads are not recommended because fiber debris increases scratch density. After 72 h of idle time, the slurry in the day tank must be purged and replaced, and the tank must be rinsed with ultrapure water followed by 0.5% hydrogen peroxide solution to remove adsorbed ruthenium species. Spent slurry discharged from the tool must be evaluated for oxidizer content before neutralization; the periodate residual must be below 5 mg/L before conventional wastewater treatment.
Lot qualification includes drawing three samples per container from top, middle, and bottom after 30 min of gentle agitation. The mean difference in D50 among sampling ports must not exceed 3 nm per ISO 22412:2017. If a container fails this homogeneity criterion, the entire lot is recalled for rework. Each shipment includes a certificate of analysis with the lot number, date of manufacture, oxidizer concentration, and the measured values for the parameters in Table 1. Electronically stored batch records are retained for 10 years under ISO/IEC 17025:2017 document control. The container is a high-density polyethylene carboy with a fluoropolymer liner; the inner liner is verified for metal extractables by inductively coupled plasma mass spectrometry after 7 days of product contact at 40 °C. This kind of lot release and extractables data is intended to support qualification in advanced-node fabs where trace metal contamination budgets are below 1×10¹⁰ atoms/cm².