| HS Code | 563476 |
| Chemical Type | Alkaline/surfactant-based aqueous cleaner |
| Appearance | Clear colorless to pale yellow liquid |
| Odor | Mild, characteristic |
| Ph At 25c | 11.5 - 12.5 |
| Specific Gravity At 25c | 1.18 - 1.25 |
| Viscosity At 25c Cp | 2.0 - 4.0 |
| Water Content | < 0.5 |
| Metal Impurity Na Ppm | < 0.1 |
| Metal Impurity Fe Ppm | < 0.1 |
| Metal Impurity Cu Ppm | < 0.1 |
| Metal Impurity Zn Ppm | < 0.1 |
| Particle Count 0 5um Per Ml | < 100 |
| Boiling Point C | 100 - 104 |
| Flash Point C | None (non-flammable aqueous) |
| Etch Rate On Cu Nm Per Min | < 0.5 |
| Etch Rate On Al Nm Per Min | < 1 |
| Etch Rate On Pi Nm Per Min | < 0.5 |
| Etch Rate On Ito Nm Per Min | < 0.5 |
As an accredited Cleaner (Cu/ Al/ PI/ ITO process) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 1-gallon HDPE bottles and 5-gallon pails; electronic/EL grade cleaner for Cu/Al/PI/ITO processes, ensuring purity. |
| Container Loading (20′ FCL) | One 20′ FCL container transporting Electronic/EL Grade Cleaner, safely packed for Cu/Al/PI/ITO processing chemicals. |
| Shipping | Ship as a liquid electronic-grade cleaner intended for Cu/Al/PI/ITO process applications. Use sealed, corrosion-resistant containers with proper cushioning. Avoid contact with incompatible materials, heat, or ignition sources. Label clearly, keep upright, and follow applicable hazardous goods regulations. Ensure ventilation and secondary containment during transit to prevent leakage or contamination. |
| Storage | Store in a tightly sealed, original container in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep separate from acids, oxidizers, and incompatible chemicals. Maintain temperature stability, prevent moisture ingress, and ensure container integrity. Always follow label/SDS instructions and local regulations for safe handling. |
| Shelf Life | Typically 12 months from manufacture if stored unopened in original container at room temperature, away from moisture and sunlight. |
In copper dual-damascene post-CMP cleaning, the copper-specific fluid is diluted 1:12–1:18 v/v with 18.2 MΩ·cm electron-grade DI water meeting ASTM D5127-13 Type E-1. The working bath is held at pH 8.6–9.2 through a polycarboxylate-buffered alkanolamine system; within this window, CuO and Cu(OH)2 dissolution proceeds via chelation rather than acid attack, while blanket physical-vapor-deposited copper etch remains below 0.5 Å/min as monitored by sheet-resistance shift. Cleaning is executed on a single-wafer spin processor fitted with 0.2 µm PTFE point-of-use filtration and 950 kHz megasonic transducers delivering 0.8–1.2 W/cm². The sequence is 60–90 s at 30°C, followed by a 45 s DI rinse at 22°C to suppress redeposition of Cu-BTA complex. The formulation removes residual benzotriazole inhibitor films, ceria or silica abrasive agglomerates, and CuO/Cu(OH)2 from the Cu surface without measurable change in Ta/TaN barrier thickness or ultralow-k SiCOH dielectric k-value beyond ±1.5%. Surface acceptance for subsequent barrier deposition is a post-clean water contact angle of ≤ 10° and an XPS Cu(OH)2 peak area not exceeding 5% of the total Cu 2p3/2 envelope. The concentrate is filled under ISO 14644-1:2015 Class 5 cleanroom conditions, membrane-filtered to 0.05 µm, and specified at total trace-metal loading ≤ 50 ppb by ICP-MS after mass preconcentration. REACH registration under Regulation (EC) No 1907/2006 and absence of Substances of Very High Concern listed in Annex XIV are documented in the compliance file; packaging materials are selected for low extractables in accordance with SEMI F57-1001 criteria for chemical distribution components. Process boundaries include the prohibition of use on exposed aluminum; at the working pH, aluminum undergoes dissolution as AlO2−, so mixed Cu/Al wafers require the dedicated aluminum-compatible grade. Bath life is terminated at whichever occurs first of 8 h, pH drift of ±0.2 from setpoint, or cation loading elevated to 500 ppb.
Aluminum pad conditioning after passivation etch is a narrower processing window than Cu post-CMP cleaning because the exposed pad must be free of fluorine-bearing etch residues and native Al2O3 while adjacent Cu traces and nitride passivation remain unetched. The aluminum-compatible grade is diluted 1:20–1:25 v/v with DI water, buffered to pH 4.5–5.0 using fluoride-free organic acid components, and applied in a batch immersion tool at 25°C with 40 kHz ultrasonic agitation for 45–60 s. In this window, Al2O3 removal proceeds at 8–12 Å/min, exposed copper etch is limited to ≤ 0.2 Å/min through a benzimidazole-type inhibitor, and silicon-nitride passivation thickness change remains below 5 Å per cycle. Post-clean qualification for wire bonding uses AFM roughness Ra < 1.0 nm and XPS fluorine 1s signal at the pad periphery below the detection limit. The finished pads support 45 µm pitch Cu wire bonding on automotive MCU devices with pull-strength acceptance per MIL-STD-883 Method 2011.9. Concentrate packaging is under ISO 14644-1:2015 Class 5, total alkali and alkaline-earth metals are controlled to ≤ 30 ppb each by ICP-MS, and the cleaner is REACH-registered under Regulation (EC) No 1907/2006. Bath life in high-mix wire-bond fabs is terminated at 6 h or 250 wafer batches, whichever occurs first; ultrasonic energy must be validated by aluminum etch-rate coupon rather than conductivity alone.
Laser-drilled or plasma-etched polyimide vias accumulate carbonized sidewall residue and buried Ti/Cu oxide debris, which cannot be removed by aqueous alkaline solutions above pH 11.5 without swelling the polyimide matrix. The PI-process fluid is diluted 1:8–1:10 v/v with DI water, set to pH 10.5–11.2, and used at 40°C for 5–10 min in a recirculating immersion bath equipped with 0.1 µm filtration and nitrogen sparge to limit hydroxylamine oxidative loss. The active chemistry combines a short-chain alkanolamine with a quaternary ammonium hydroxide and a sulfonate-bearing chelate; this removes carbonized PI residue without causing measurable via enlargement, as confirmed by top-down SEM diameter change ≤ 0.5 µm at 20 µm via target. Cured polyimide thickness increase after the maximum 10 min exposure is held to ≤ 3% by ellipsometry, and the film retains ≥ 95% of its initial elongation at break when tested per ASTM D882-18 on a free-standing film. The cleaned vias are then subjected to electroless copper seed deposition or TiW sputtering; pull-strength after electroless Cu plate-up is specified at ≥ 0.35 kgf/mm² for chip-on-film packages with 18 µm line/space. Electronic/EL-grade controls include low sodium and potassium, each ≤ 20 ppb in concentrate, to avoid mobile ion drift in polyimide under bias humidity testing at 85°C/85% RH per JEDEC JESD22-A101C. Process limitations are narrow: above 45°C, polyimide swelling increases nonlinearly, and below 35°C, residue removal time extends beyond 10 min, increasing bath decomposition products. The bath is discarded after 4 h of accumulated immersion time because hydroxylamine decomposition reduces cleaning activity even when pH is replenished.
Before photoresist coating on ITO transparent anodes, the ITO pre-clean grade is diluted 1:25–1:30 v/v with DI water, buffered at pH 7.8–8.2, and applied at 30°C for 60 s in a spin-spray tool with 0.1 µm point-of-use filtration. The formulation removes adsorbed organic contamination, airborne molecular contamination residues, and the thin carbonaceous layer left by previous air exposure, while limiting indium dissolution to ≤ 1.0 ppb/min as measured by ICP-MS on a 100 cm² ITO coupon. Sheet-resistance shift after cleaning is specified as ≤ 0.5% relative to the pre-clean four-point probe value, and the DI water contact angle is reduced to ≤ 5° for resist adhesion. The process applies to top-emission OLED backplane fabrication; cleaned ITO substrates with 2 µm pixel pitch are coated with positive photoresist and patterned to define anode islands. Post-clean surface roughness measured by AFM is held at Ra < 2.0 nm to avoid point-anode field enhancement. Compliance of the pre-clean grade is specified with total chloride and sulfate ≤ 50 ppb each by ion chromatography, and the material is filtered through 0.05 µm membranes under ISO 14644-1:2015 Class 5 cleanroom before shipment. This chemistry must not be used after ITO wet etching because residue ions are different; the post-etch residue grade described below is required.
ITO wet etching with oxalic acid-based or HCl/HNO3 mixtures leaves tin oxide-rich nanoparticles and indium chloride/hydroxide residues that redeposit along pattern edges. The post-etch ITO residue grade is diluted 1:12–1:15 v/v with DI water, adjusted to pH 8.8–9.5, and used at 35°C for 180 s in an ultrasonic immersion tank at 40 kHz with 0.2 µm recirculating filtration. The cleaner combines a chelating monocarboxylate with an ethoxylated wetting agent to lift tin oxide nanoparticles from the pixel-electrode gap without attacking underlying silicon oxide or aluminum gate metal; aluminum etch is specified below 2 Å/min at pH 9.0, and above pH 9.5 aluminum protection is lost, so pH control is the primary process limit. Post-clean residue verification uses dark-field microscopy with residual particle count ≤ 10 particles/cm² at ≥ 0.3 µm size bin and TXRF total surface tin below 1.0×10¹⁰ atoms/cm². The terminal devices are TFT-LCD pixel arrays with 5 µm channel-passivation overlap tolerance; incomplete residue removal leads to leakage-current drift in final panel inspection. The concentrate is manufactured under ISO 14644-1:2015 Class 5 and specified with total trace-metal impurities ≤ 50 ppb; the product file includes REACH conformance under Regulation (EC) No 1907/2006. The bath is replaced after 6 h or when total tin loading reaches 1 ppm, because tin accumulation accelerates redeposition at the pH 9.0–9.5 operating point.
Cu pillar and RDL structures require removal of post-etch residue, Cu2O, and metallic halide corrosion products immediately before solder paste printing or ball drop. The copper pillar grade is diluted 1:8–1:10 v/v with DI water, pH is held at 4.8–5.2 with a fluoride-free organic acid buffer, and the fluid is applied through an inline spray chamber at 35°C for 120 s with nozzle pressure 1.0–1.2 MPa. This window dissolves Cu2O at 15–25 Å/min while protecting SnAg cap metallurgy through a heterocyclic inhibitor; cap thickness measured by XRF remains within ±0.1 µm after two process cycles. The cleaned wafer proceeds to flip-chip attach; bump shear strength after reflow is specified as ≥ 6.0 g/mil² per JEDEC JESD22-B117A for 40 µm pitch Cu pillars with SnAg caps. For RDL lines with 2 µm line/space, post-clean surface oxidation is controlled by a nitrogen-pressurized buffer tank and a final DI rinse at 1.5 MPa to prevent water spotting. The fluid must not contact exposed ITO because the acidic pH etches indium oxide; mixed substrates require process flow segregation. The packaging grade is supplied with SEMI F57-1001-compliant wetted surfaces and total trace-metal impurities ≤ 50 ppb. Bath life in high-volume wafer-level packaging is set at 8 h or 500 panels, whichever occurs first, and is verified by pH drift ±0.2 and Cu concentration ≤ 100 ppm.
Flexible hybrid circuits that carry Cu traces, Al bond pads, and ITO sensor traces require a single clean step to avoid sequential chemistry damage; the mixed-metal application uses the aluminum-compatible grade at a reduced dilution of 1:30 v/v and a short 30 s contact at 22°C, with pH 4.5–5.0, followed by immediate DI rinse. This condition removes aluminum oxides and trace ionic contamination while keeping copper etch below 0.5 Å/min and ITO sheet-resistance shift below 2%. The process is run in a single-chamber spin-spray tool with perfluoropolymer fluid paths to avoid metal leaching; terminal devices are biomedical sensor arrays and smart-label circuits with 25 µm feature pitch. The constraint is that this diluted condition does not remove heavy Cu2O or PI post-laser residue, so it is limited to light surface preparation after lamination or singulation. Concentrate compliance for the mixed-metal application mirrors the Al pad grade: ISO 14644-1:2015 Class 5 filling, total alkali metals ≤ 30 ppb, and REACH registration under Regulation (EC) No 1907/2006.
| Process | Dilution | Temperature | Contact time | Critical control |
|---|---|---|---|---|
| Cu dual-damascene post-CMP | 1:12–1:18 | 30°C | 60–90 s | pH 8.6–9.2 / Cu etch ≤0.5 Å/min |
| Al pad conditioning | 1:20–1:25 | 25°C | 45–60 s | pH 4.5–5.0 / Al2O3 etch 8–12 Å/min |
| PI via residue | 1:8–1:10 | 40°C | 5–10 min | PI swell ≤3% |
| ITO pre-coating | 1:25–1:30 | 30°C | 60 s | In dissolution ≤1.0 ppb/min |
| ITO post-etch residue | 1:12–1:15 | 35°C | 180 s | pH 8.8–9.5 / Sn ≤1×10¹⁰ atoms/cm² |
| Cu pillar/RDL pre-bump | 1:8–1:10 | 35°C | 120 s | pH 4.8–5.2 / SnAg cap Δ≤0.1 µm |
| Mixed Cu-Al-ITO light clean | 1:30 | 22°C | 30 s | Cu etch ≤0.5 Å/min / ITO ΔR≤2% |
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The product designated Cleaner (Cu/Al/PI/ITO process) Electronic/EL Grade is an aqueous-organic, near-neutral, fluoride-free process liquid formulated for post-etch residue removal and pre-deposition surface conditioning on substrates carrying copper, aluminum, polyimide, and indium tin oxide. Representative physical and chemical specifications are: pH 7.2–7.8 at 25 °C, specific gravity 1.01–1.03, kinematic viscosity 2.4–3.1 mm²/s at 25 °C, and closed-cup flash point above 93 °C. The liquid is filtered to 0.05 µm and filled under ISO 14644-1:2015 Class 5 conditions. Metal impurity ceilings are ≤5 ppb each for sodium, potassium, iron, and copper by ICP-MS; chloride and sulfate are controlled to ≤50 ppb. The product contains no intentionally added fluoride, no sodium or potassium hydroxides, and no glycol ethers restricted under REACH 1907/2006 Annex XVII. Because the formulation is buffered near neutral, it can be applied to wafers, panels, and flex substrates where single-metal cleaners either etch aluminum, oxidize copper, or degrade indium tin oxide.
The cleaner is used in TFT-LCD photolithography after dry etch, before ITO and aluminum interconnect deposition, and in chip-on-panel packaging where the dielectric is polyimide. In these flows, the sequence is typically post-ash rinse, cleaner immersion or spray, ultrapure water rinse, and spin-dry. The product is compatible with both batch immersion wet benches and single-wafer spray processors; process conditions vary from 25 °C to 45 °C and from 1:20 to 1:50 dilution depending on residue loading. A representative working bath at 35 °C and 1:30 dilution reduces the contact angle of a post-ash polyimide surface from 35° to ≤8° within 60 s, as measured by sessile drop goniometry. The same bath removes thermal oxide from copper with an etch rate below 1.5 Å/min, which is small enough to preserve 300 nm seed layers. For aluminum pads, the product leaves less than 0.5 nm roughness increase after 30 min immersion as measured by atomic force microscopy.
Mixed-material cleaning imposes a narrower pH envelope than single-metal cleaning. Aluminum dissolution accelerates below pH 4.0 and above pH 9.5 because the amphoteric oxide dissolves; copper oxidation in aerated alkaline baths becomes significant above pH 8.5. Indium tin oxide loses tin at pH ≤3.5 in acidic chelating media, while polyimide hydrolysis accelerates in alkaline baths above 45 °C. The product operates in the post-dilution pH range 7.0–7.4, where copper and aluminum etch rates remain below 1.5 Å/min and 2.0 Å/min, respectively, at 35 °C over 30 min by ASTM G31-72 coupon immersion. The pH range is maintained by a polycarboxylate buffer system rather than inorganic phosphates, thereby avoiding phosphate redeposition on copper seed.
In immersion tools with recirculation at 20 L/min and ultrasonic transducers at 40 kHz, the controlling failure mode is not direct bulk etch but galvanic exchange between exposed copper and aluminum when bath conductivity exceeds 1.2 mS/cm and dissolved copper reaches 80 ppm. The chelating package is selected to bind Cu(I) and Cu(II) and to limit electroless displacement onto aluminum pads, but bath life is deliberately constrained to 48 h in immersion cells because accumulated copper and chloride increase the open-circuit potential difference. A laser profilometer on production 200 mm wafer test vehicles showed aluminum bond pad recess increasing from 0.8 nm/min to 2.4 nm/min when dissolved copper rose from 30 ppm to 90 ppm at 35 °C. The maximum bath temperature is 45 °C; above this, polyimide swelling and ITO surface roughening become measurable. The maximum ultrasonic energy density is 12 W/L; above this, cavitation damage on 20 µm polyimide cantilevers has been observed as edge chipping.
| Material | Condition | Measured threshold | Reference method |
|---|---|---|---|
| Cu seed | 35 °C, 30 min | ≤1.5 Å/min | ASTM G31-72 |
| Al bond pad | 35 °C, 30 min | ≤2.0 Å/min | ASTM G31-72 |
| Polyimide passivation | 45 °C, 20 min | ≤0.4% thickness loss | ASTM D7127 |
| ITO layer 135 nm | 35 °C, 10 cycles × 5 min | ≤1.0% sheet-resistance shift | four-point probe |
The electrochemical potential of the bath, measured against an Ag/AgCl reference electrode, remains between -0.15 V and +0.05 V at 35 °C, a range in which copper is passivated and aluminum remains in its oxide-protected state. When the cleaner is diluted with recycled water containing chloride above 2 ppm, the potential shifts positive and pitting on aluminum pads can initiate within 10 min. This is the reason for specifying fresh ultrapure water above 18 MΩ·cm resistivity rather than reclaimed UPW.
For indium tin oxide layers of 120–150 nm thickness, the relevant damage metric is not bulk dissolution but sheet-resistance shift after cumulative cleaning cycles. A four-point probe measurement of 135 nm ITO exposed to 10 cleaning cycles at 35 °C for 5 min per cycle shows sheet-resistance change below 1.0% when dissolved tin is maintained below 0.3 ppm. If dissolved tin rises above 1.0 ppm, the shift increases to 3–5%, and surface carbon increases to 8–12 at% by XPS. The mechanism is chelator and surfactant adsorption on oxygen-vacancy-rich ITO surfaces, followed by tin-enriched oxide formation. The product therefore uses a low-adsorbing nonionic surfactant with cloud point above 85 °C and a tin-selective complexing agent with log K 8–10; this range is high enough to prevent tin hydroxide precipitation but low enough to avoid bulk ITO leaching. On polyimide passivation, the cleaner maintains thickness loss below 0.4% after 20 min at 45 °C by profilometry according to ASTM D7127. The cleaned polyimide surface retains a deionized water contact angle below 10° after 60 s at 25 °C, which permits subsequent photoresist adhesion. For polyimide cured above 350 °C, the product does not soften or craze the polymer; however, a two-stage rinse is required with final rinse resistivity above 18 MΩ·cm at 20–25 °C to remove the adsorbed surfactant film. If the rinse temperature is below 15 °C, residual organic film can remain and cause variable adhesion on subsequent spin-on dielectrics.
Point-of-use filtration is required. The liquid is compatible with fluoropolymer, polypropylene, and electropolished stainless steel wetted parts; bare aluminum and copper alloy fittings are incompatible because long-term contact extracts metal ions. In recirculation loops, the product is maintained at 20 ± 2 °C with a 0.05 µm polytetrafluoroethylene membrane filter and pressure drop below 0.7 bar; particle counts remain below 100 particles/mL at 0.3 µm using ISO 21501-4. Immersion bath life is limited to 48 h or 2,000 substrates/L, whichever occurs first. In single-wafer spray tools, the product is dispensed at 0.8–1.2 L/min through fan nozzles at 1.5 bar, with residence time of 45–90 s. The main contamination source is not the as-supplied chemical but inline mixing and operator handling; the product is therefore supplied in 20 L fluoropolymer canisters with nitrogen blanketing at 0.2 bar.
In recirculation loops, the accumulation of dissolved tin at 1.0 ppm correlates with ITO particle adhesion and subsequent cleaning efficiency loss. The solubility limit of the tin complex is approximately 12 ppm at 20 °C; above this, tin oxide precipitation is observed on tank walls and can be minimized by maintaining pH 7.2–7.4. The chelating system does not flocculate at the working pH, but exposure to cation exchange resins removes the buffer and chelator, causing the bath pH to fall below the aluminum stability boundary.
In spray processing, the cleaner is diluted 1:10 to 1:40 with ultrapure water and delivered at 0.8–1.2 L/min; physical droplet momentum removes particulate debris without the extended liquid contact that aggravates galvanic attack. Immersion processing is preferred for high-aspect-ratio via cleaning because it provides continuous wetting of recessed surfaces, but it requires stricter control of dissolved copper and chloride. The formulation’s surfactant package has a dynamic surface tension below 30 mN/m at 1 s surface age by maximum bubble pressure, enabling wetting of 5–10 µm via openings. In comparison with conventional single-metal copper cleaners, the product avoids strong alkaline conditions and fluoride, reducing aluminum pad attack. In comparison with ITO-contact cleaners containing aggressive acidic salts, it leaves lower chloride residues, measured below 1 × 10¹² atoms/cm² by TXRF after rinse. The trade-off is a slightly lower oxide removal rate: heavy cupric oxide requires immersion at 40 °C with 40 kHz ultrasonics, which may be incompatible with delicate polyimide cantilever structures. Field data from flat-panel lithography lines show a change in visual residual defects on aluminum pads from 2.4 defects/cm² to 0.7 defects/cm² after substitution when paired with a 0.5 µm rinse filter; however, published data for this specific configuration is limited and local tool geometry influences the result.
Compliance verification against the following matrix is performed on each lot or on a reduced-frequency protocol with full documentation. The analytical methods and limits are applied to the as-supplied liquid and, where indicated, to the diluted working bath. The product is supplied with a certificate of analysis reporting pH, specific gravity, particle count, and the metal impurity panel.
| Requirement | Method | Parameter | Limit |
|---|---|---|---|
| RoHS 2011/65/EU | IEC 62321-5 | Cd | 100 ppm |
| RoHS 2011/65/EU | IEC 62321-4 | Hg | 1,000 ppm |
| RoHS 2011/65/EU | IEC 62321-5 | Pb | 1,000 ppm |
| REACH 1907/2006 Annex XVII | GC-MS | Benzene | 0.1 wt% |
| SEMI C63 | ICP-MS | Na, K, Fe, Cu | ≤5 ppb each |
| ISO 14644-1:2015 | Laser particle counter | Fill environment | Class 5 |
The operational boundaries are: dilution with ultrapure water above 18 MΩ·cm resistivity, bath temperature below 45 °C, and avoidance of mixing with fluoride-containing strippers or strong oxidizing acids. Mixing with hydrogen peroxide or ozonated water can shift the pH and produce oxygenated copper surfaces; mixing with acid-stripper residues can reduce pH below 4.0 and initiate aluminum attack. The product is not intended for vapor degreasing or for closed-loop systems with cation exchange resins because loss of the buffer system can alter the pH window and metal compatibility.