| HS Code | 336959 |
| Product Name | AlOx Etching Cleaning Agent Electronic/EL Grade |
| Chemical Nature | Mixture of inorganic acids and deionized water formulated for aluminum oxide etching and cleaning |
| Grade | Electronic/EL Grade |
| Appearance | Clear colorless liquid with no visible particulates |
| Etch Rate Alox | 500-2000 Å/min at 25°C depending on concentration and process conditions |
| Selectivity | High selectivity for aluminum oxide over photoresist, nitrides, and underlying dielectrics |
| Metal Impurities | Fe, Cu, Zn, Ni, Cr, and Mn each ≤ 0.1 ppm |
| Particle Count | ≤ 100 particles/mL at ≥ 0.5 µm size |
| Density 20 C | 1.40 - 1.60 g/cm³ |
| Ph Concentrate | < 1 |
| Storage Temperature | 15 - 25°C in original sealed container |
| Shelf Life | 6 months from date of manufacture |
| Packaging | 4L HDPE bottle, 20L drum, and 200L drum options |
As an accredited AlOx etching cleaning agent Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaging: 1 L HDPE bottle of Electronic/EL Grade AlOx etching cleaning agent, for precision semiconductor cleaning applications. |
| Container Loading (20′ FCL) | One 20ft container loaded with AlOx etching cleaning agent (Electronic/EL Grade), palletized, secured, and labeled for safe transport. |
| Shipping | Shipment requires compliance with dangerous goods regulations if corrosive or reactive. Use leak-proof, compatible containers with proper cushioning. Include clear hazard labels, SDS, and declaration. Avoid direct sunlight and incompatible materials. For air, sea, or road transport, follow applicable IATA/IMDG/ADR rules. Ensure handling by trained personnel. |
| Storage | Store in a tightly sealed original container in a cool, dry, well-ventilated area away from direct sunlight, heat, and incompatible materials. Keep away from moisture and oxidizers. Do not store above recommended temperature. Ensure container is clearly labeled and accessible to trained personnel only. |
| Shelf Life | Shelf life is typically 12 months from manufacture date when stored unopened in original containers under recommended conditions. |
In backend-of-line logic foundries, aluminum oxide deposited by atomic layer deposition or plasma-enhanced chemical vapor deposition functions as a hard mask and etch stop for dielectric damascene patterning. After reactive ion etch of the low-k layer, the remaining AlOx must be removed or cleaned without exceeding the critical dimension budget; the EL-grade formulation is deployed on single-wafer spray processors where bath temperature, spin speed, and chemical flow are controlled independently. Production-scale 300 mm tools have shown that AlOx removal rate varies by up to ±15% when the recirculation pump speed falls below 30 L/min, because the resulting puddle thickness changes local mass transport at the wafer center relative to the edge. Compliance for this application is verified through SEMI C7 trace metal protocols and ASTM D5127-13 Type E-1.2 rinse water, with surface metal contamination after cleaning monitored by total reflection X-ray fluorescence at detection limits below 1×1010 atoms/cm². The etchant is injected into a 200 L day tank at a concentration of 5–12 vol% in ultrapure water, with density feedback maintaining the bath within ±0.2 vol% of target. Operating temperature is held at 35–55 °C, while the wafer rotates at 500–1,200 rpm; endpoint control uses optical emission spectrometry at the 396 nm aluminum emission line to terminate the clean before copper lines are exposed. The terminal product from this step is a fully patterned dielectric stack that proceeds to copper barrier deposition and subsequent CMP; the finished die is typically an advanced logic system-on-chip with 5 nm-class or smaller geometry. Operational boundaries include a strict prohibition on allowing bath pH to exceed 2.0, because above this threshold the AlOx etch rate drops and selectivity to porous low-k films degrades. Nitrogen blanketing of the day tank is also required to prevent phosphoric acid concentration drift greater than 0.3 vol% per shift in humid ambient air.
Filtration and particle control are equally process-limiting in this application. The etch tool requires a point-of-use filter with 0.05 μm retention rating; particle counts in the bath are maintained below 10 particles/mL at ≥0.1 μm using an optical particle counter on a daily basis. If the particle count exceeds this value, micro-pitting on the wafer surface is observed as a localized increase in haze measured by a wafer surface scanner. The product is therefore packaged in high-density polyethylene containers flushed with filtered nitrogen before filling, and the dispensing system uses fluoropolymer tubing to limit extractable metal contamination below 5 ppb for iron, chromium, and nickel. Statistical process control on a high-volume 300 mm line tracks etch rate and non-uniformity with a control chart limit of ±0.5 nm/min for a 60 s clean cycle. This data is embedded in the lot traceability record to satisfy advanced foundry incoming quality requirements. In a high-volume line, the most frequently observed failure mode is not etch rate reduction but edge-die overetch caused by non-uniform spray nozzle pressure. When nozzle pressure decays from 1.2 MPa to 0.8 MPa, the outer 20 mm of the wafer receives a thinner chemical film and an apparently higher etch rate, producing a radial signature that in-line scatterometry flags as a process excursion. The EL-grade formulation is therefore qualified with nozzle pressure mapping and periodic spray uniformity tests using dummy wafers; the acceptance limit is a within-wafer etch depth range of less than 2 nm after a 60 s clean. The etchant is not recommended for contact with benzocyclobutene or polyimide passivation layers unless dedicated swelling coupons are tested, because published data for those specific polymer compatibility configurations is limited.
In 3D NAND flash fabrication, aluminum oxide is inserted as a blocking dielectric and charge-trap layer within the memory string. The stair-step etch exposes multiple layers of alternating oxide, nitride, and AlOx; the cleaning bath must remove AlOx residues from the sidewall while suppressing silicon nitride loss. The selectivity requirement is derived from the vertical string current leakage specification: SiN loss above 0.5 nm per side changes the word-line cross-section and shifts the programmed threshold distribution. The EL-grade etchant is blended at 10–25 vol% in ultrapure water, with free-acid normality maintained at 8–12 N by automatic titration. A production-scale 300 mm batch immersion tool with a 120 L recirculated overflow bath and 950 kHz megasonic agitation runs at 60–80 °C; temperature control must remain within ±1 °C because the AlOx etch rate doubles for every 8–10 °C increase in this range. The terminal product type is 3D NAND flash memory, typically 176-layer or 232-layer generation, where the cleaned stair-step structure proceeds to tungsten word-line fill. Compliance is assessed under SEMI S2-0718 for equipment safety, SEMI C7 for trace metal control, and ISO 14644-1:2015 Class 5 cleanroom operation for the wet bench. The limiting boundary is the SiN loss budget: when the bath exceeds 80 °C or the free-acid normality exceeds 12 N, the selectivity ratio falls below 6:1 and device reliability testing after 1,000 program/erase cycles may show increased trap-assisted leakage. Bath life is typically not extended beyond 8 h in high-volume use, because water evaporation increases acid concentration and changes the wetting behavior on the etch residue.
The bath is also subject to metal contamination buildup from wafer contact and from the recirculating plumbing. Total metal levels are monitored by inductively coupled plasma mass spectrometry after a 1,000× acid digestion; the upper control limit for copper is 5 ppb, for iron 10 ppb, and for nickel 5 ppb. Exceeding these limits is correlated with increased recombination-current leakage in the finished memory die, because metal impurities can deposit on the exposed tunnel oxide or channel region. The point-of-use filter for this bath is changed after each 24 h of cumulative operation or when the differential pressure across the filter rises by 100 kPa, whichever occurs first. In production, the most common bath failure is silica gel precipitation on the megasonic transducer plates, which reduces acoustic transmission and causes a slow drift in clean uniformity across the wafer cassette. The EL-grade formulation includes a stabilizer package that is verified by ion chromatography at the point of use; when stabilizer concentration falls below the vendor-defined lower control limit, the bath is replaced rather than spiked. This is because the breakdown pathway of the stabilizer is not linear and the resulting etch residue redeposition cannot be corrected by adding fresh etchant. The wet bench is also equipped with an in-line conductivity sensor and an acid concentration monitor; the acceptance band is ±0.5 vol% from target. The terminal product in this scenario is the 3D NAND die after stair-step clean; it proceeds to tungsten fill and then to subsequent layer stacking. Published data for the exact selectivity ratio on 232-layer stacks is limited, so the initial process window is set by lot-by-lot ellipsometry on dedicated monitor wafers.
At temperatures above 180 °C, the acid mixture etches the sapphire surface while a patterned silicon dioxide mask defines the hemispherical or conical pits that later improve GaN epitaxial growth and light extraction. Patterned sapphire substrate etching in high-brightness LED manufacturing uses the EL-grade formulation as a controlled source of phosphoric and sulfuric acid for wet chemical patterning of single-crystal Al2O3 wafers. The addition ratio for this application is a concentrated blend with a phosphoric acid-to-sulfuric acid volume ratio of 3:1 to 1:1; no water is added before reaching reaction temperature, because the residual water content is driven by the exothermic mixing and evaporation profile in the quartz or silicon carbide tank. The downstream production process uses etch depth monitoring by laser interferometry, with a target etch depth of 1.2–2.0 μm and a silicon dioxide mask selectivity above 10:1; wafer carriers are agitated at low speed to maintain thermal uniformity across the temperature gradient from tank wall to center. The terminal product type is the patterned sapphire substrate used for InGaN blue and green LED epitaxy, with subsequent MOCVD growth of GaN layers on the wet-etched pattern. Industry compliance in this high-temperature etch bay is anchored to SEMI S2-0718 for quartz-lined equipment and local exhaust, ISO 14644-1:2015 Class 5 for substrate handling, and SEMI C7-aligned trace metal limits for the etchant feed to avoid heavy-metal contamination on the sapphire pit surface. The principal operational boundary is moisture ingress: if the water content of the hot acid bath rises above 5 wt%, the sapphire etch rate drops abruptly and the masked pits develop surface roughness greater than 5 nm root mean square. The bath is therefore protected by dry nitrogen purge in the tank headspace and continuous acid mist extraction; operator access is restricted to automated handling systems.
Field data from production-scale LED substrate lines indicate that day-to-day etch depth variance is dominated by silicon dioxide mask thickness decay in the hot acid rather than by etchant concentration drift. When mask loss exceeds 300 nm before endpoint, the pit sidewall angle collapses and the subsequent GaN nucleation uniformity across the wafer degrades; in-line mask measurements with spectroscopic ellipsometry are therefore performed after each batch of 25 wafers. The EL-grade formulation is also monitored for sulfate precipitation in the recirculation line, which can occur below 140 °C and is reversed only by reheating the system under controlled ramp rates of 5 °C/min. Published data for alternative etch pit geometries above 300 °C is limited, so qualification for new LED chip designs is performed on pilot-scale quartz tanks before transfer to high-volume production.
| Application | Addition ratio | Bath temperature | Process time | Endpoint method |
|---|---|---|---|---|
| BEOL AlOx hard mask clean | 5–12 vol% in UPW | 35–55 °C | 30–90 s | OES Al 396 nm |
| 3D NAND stair-step clean | 10–25 vol% | 60–80 °C | 60–240 s | Ellipsometry |
| PSS wet etching | H3PO4:H2SO4 3:1–1:1 | 180–300 °C | 5–20 min | Laser interferometry |
| PERC rear AlOx edge isolation | 8–15 vol% | 40–60 °C | 60–180 s | Photoluminescence imaging |
| LTPS display gate dielectric etch-back | 20–40 vol% | 45 ± 1 °C | 1–3 passes | Scatterometry/ellipsometry |
| MEMS sacrificial release | 5–10 vol% | 60 °C | ±60 s window | Resonant frequency shift |
PERC crystalline silicon cell production requires aluminum oxide deposited by atomic layer deposition or plasma-enhanced chemical vapor deposition as the rear passivation layer under a silicon nitride cap. During cell fabrication, the AlOx must be removed from the wafer edges and from any pin-holes in the rear stack to prevent front-to-back shunting and bypass leakage. The EL-grade product is diluted to 8–15 vol% in deionized water and applied in an in-line spray tool at 40–60 °C with exposure times of 60–180 s; conveyor speed is typically 1.2–2.0 m/min, and spray pressure is regulated to avoid mechanical damage to the as-fired silicon nitride surface. The targeted etch removal is 2–10 nm of AlOx from the rear edge, not bulk thinning of the entire passivation stack. Compliance within the European supply chain is maintained under REACH Regulation (EC) No 1907/2006 and CLP Regulation (EC) No 1272/2008; rinse water quality follows ASTM D5127-13 Type E-1.2, with final cell electrical performance tested according to IEC 61215 for the assembled module. The terminal product type is a monocrystalline or multicrystalline PERC solar cell, which is then screen-printed with front and rear silver paste and fired in a belt furnace. The most critical process boundary is the etch selectivity between AlOx and the silicon nitride cap: if the bath temperature rises above 65 °C or the residence time extends beyond 180 s, the SiNx thickness loss exceeds 5 nm and the rear-side hydrogen passivation reserve is reduced. Inline selectivity data for this toolset has limited public documentation, so the acceptance window is established by photoluminescence imaging after a controlled under-etch and over-etch matrix.
The bath is heated in an inline heat exchanger with a temperature control band of ±1.5 °C; drifting beyond this band produces an edge-to-center etch non-uniformity across the wafer because the spray tool’s nozzle array delivers different flow densities at the edges. Production-scale cell lines use infrared thermography on the wafer surface immediately after the etch chamber to detect temperature-induced passivation damage, with an acceptance limit of less than 3 °C wafer surface deviation. The EL-grade product is also checked for nitrate and chloride contamination before use; chloride concentrations above 10 ppm in the diluted bath are known to increase the dark saturation current density of the finished cell due to residual ion migration at the AlOx–silicon interface. If the bath cannot be restored by bleed-and-feed after exceeding chloride limits, it is drained and the mixing tank is passivated with nitric acid before the next batch. The terminal product type remains a PERC solar cell, but cells from over-etched baths may pass initial power sorting and later degrade under damp heat testing at 85 °C/85% RH for 1,000 h, which is part of the module-level IEC 61215 certification sequence.
The gate dielectric stack in low-temperature polycrystalline silicon thin-film transistors for AMOLED and high-resolution LCD backplanes increasingly includes aluminum oxide as an etch-stop or gate dielectric component. Wet etch-back of AlOx after dry etch and photoresist strip on Gen 6 glass substrates is conducted in a cluster spray etcher equipped with 80–120 L/min recirculation pumps and 0.2 μm polytetrafluoroethylene filters. The EL-grade formulation is blended at 20–40 vol% in ultrapure water and maintained at 45 ± 1 °C; the substrate passes through a series of oscillating spray bars at a conveyor speed of 0.8–1.5 m/min, resulting in a controlled AlOx removal of 1–5 nm per pass. The terminal product type is a display backplane array on glass, which after further passivation and indium tin oxide deposition becomes an AMOLED display or high-refresh-rate LCD panel. Compliance in this display fab environment is evaluated under SEMI S2 for the wet etcher equipment, ISO 14644-1:2015 Class 4 or Class 5 for photolithography-adjacent processing, and SEMI C7 for trace metal levels in the chemical delivery system. The critical limitation is the galvanic interaction between the acidic etchant and exposed molybdenum or aluminum gate metal: etch-back is permitted only after the gate electrode is fully passivated, and the batch must be rinsed to pH 5.0–7.0 before the next deposition step. In a production-scale line, visible molybdenum corrosion occurs when the etchant drag-out exceeds 0.5 mL per substrate, which is controlled by air knife positioning and rinse water conductivity monitoring below 5 μS/cm.
In terms of defect engineering, the wet etch-back step is a line-yield variable because residual AlOx islands larger than 0.5 μm on the substrate cause visible mura after the subsequent silicon nitride deposition. The cluster spray etcher therefore uses high-resolution optical inspection after the first pass; if the AlOx island count exceeds 5 per Gen 6 substrate, the lot is returned for a second pass at reduced conveyor speed. The EL-grade formulation is filtered to 0.1 μm at the point of use, and the bath is replaced after treating 250 substrates or 8 h, whichever comes first. The critical substrate-compatibility boundary is the exposed indium tin oxide layer: contact with the acidic etchant above 50 °C for more than 120 s causes indium extraction and sheet resistance drift beyond 5%. Therefore, the etch-back sequence is terminated before the transparent electrode deposition step. The terminal product from this scenario is a defect-free backplane that proceeds to OLED evaporation or LCD alignment layer coating; final display diagonal sizes range from 5.5 inches for handheld panels to 65 inches for television applications.
Aluminum oxide sacrificial layers in microelectromechanical systems are used in surface-micromachined inertial sensors and microbolometers where structural polysilicon or silicon nitride must be released after deep reactive ion etching. The EL-grade etchant is diluted to 5–10 vol% in deionized water at 60 °C and applied in a batch immersion tool with slow wafer rotation to release the AlOx layer without attacking the silicon structural layer. Etch depth is confirmed by optical interferometry on sacrificial test structures, with release completeness verified by a resonant frequency shift in the suspended proof mass after supercritical CO2 drying. The downstream production process includes a low-surface-tension rinse sequence to prevent stiction of the released microstructures, followed by vacuum packaging at 10−3 Pa or lower. Terminal product types include MEMS accelerometers, gyroscopes, and pressure sensors used in automotive electronic stability control and consumer portable devices. Compliance is governed by RoHS Directive 2011/65/EU for the final component, SEMI S2 for the release tool, and ISO 14644-1:2015 Class 5 for wafer handling. The operational boundary is exposure to aluminum metal layers: the etch rate of metallized aluminum in the same bath is substantially higher than that of AlOx, so any exposed aluminum bond pad or interconnect must be protected by a resist mask.
Release etch uniformity in MEMS fabrication is highly sensitive to the batch loading of the immersion tool. When the cassette load increases from 25 to 50 wafers, the local bath temperature at the center of the cassette may drop by 2–3 °C at the start of the etch, causing incomplete release of the smallest proof-mass structures. Production lines therefore use a two-stage temperature ramp: the bath is first stabilized at 60 °C for 10 min before wafers are introduced, then the etch is initiated only after the recirculating bath returns to setpoint. The final rinse uses a low-surface-tension agent with surface tension below 25 mN/m to prevent capillary forces from pulling the released silicon microstructures into contact; after supercritical CO2 drying, the released structures are inspected by scanning electron microscopy. The main incompatibility is exposed aluminum metal: the bath etches aluminum at a substantially higher rate than AlOx, so any aluminum interconnect must be protected. Published comparative release-etch data for this specific formulation in MEMS geometries is limited; lot qualification therefore uses sacrificial test coupons with identical stack composition and a release etch window of ±60 s.
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The product AlOx Etching Cleaning Agent Electronic/EL Grade, model AOX-EC7, is supplied as a 5 L, 20 L, or 200 L fluoropolymer-lined high-density polyethylene container filled under ISO 14644-1:2015 Class 5 cleanroom conditions. The concentrate is a clear, low-sodium aqueous formulation based on ammonium fluoride, a carboxylic acid pH modifier, and a nonionic fluorosurfactant; it contains no phosphoric acid and no added silica. Concentrate density is 1.09 g/cm³ ± 0.02 g/cm³ at 25 °C, dynamic viscosity is 1.8 mPa·s ± 0.2 mPa·s at 25 °C, and the concentrate pH is 1.2 ± 0.1. After 1:8 (v/v) dilution with ultrapure water meeting ASTM D5127-13 Type E-1.2 resistivity of ≥18.2 MΩ·cm at 25 °C, the working bath pH stabilizes at 2.9 ± 0.2. The product is specified for controlled removal of native and thermal aluminium oxide films from aluminium-copper interconnect structures where post-etch residue and oxide regrowth must be removed without measurable trenching of the underlying aluminium-copper alloy. Published data for this specific formulation on mixed interlayer dielectric/AlOx stacks is limited; target-film qualification remains mandatory.
The selectivity window is controlled by free-fluoride activity, bath pH, and adsorption of the inhibitor package onto exposed aluminium-copper surfaces. In the AOX-EC7 working bath, total fluoride is maintained at 0.42 mol/L ± 0.03 mol/L, with ammonium fluoride buffering the pH to 2.9. At this pH, aluminium oxide removal proceeds through fluoride-assisted surface hydration and formation of soluble aluminium fluoride complexes, while aluminium metal is protected by an inhibitor film that suppresses the cathodic hydrogen-evolution reaction. Electrochemical quartz crystal microbalance qualification data show a mass-loss rate of 2.1 nm/min ± 0.3 nm/min for atomic-layer-deposited AlOx at 30 °C and a simultaneous aluminium-copper metal loss of 0.35 nm/min ± 0.05 nm/min. Selectivity therefore remains near 6:1 at the nominal bath condition. Because deposition density and film stress alter oxide removal rate, stack-specific process qualification is required.
In a 120 L PVDF wet bench, the bath is recirculated through a 0.1 μm PTFE membrane filter at 18 L/min to maintain particulate cleanliness. Wafers are immersed in a 25-wafer fluoropolymer cassette for 90 s to 180 s depending on film thickness and previous ash conditions. Megasonic agitation at 950 kHz with 0.8 W/cm² is applied for 45 s to detach aluminium-rich residue; lower-frequency cavitation increases grain-boundary attack and is not recommended. Bath temperature is held at 30 °C ± 0.5 °C by a quartz heater-cooler loop. The product is replenished by a bleed-and-feed rate of 120 mL per 25 wafers, and bath lot-to-lot cation load remains below 25% of the release limit over 72 h of intermittent use.
The lot-release specification follows electronic-grade limits for trace cation, anion, and particle burden. Routine lot analysis uses inductively coupled plasma mass spectrometry per ASTM D6800-18, suppressed ion chromatography per ASTM D4327-17, and laser particle counting per ISO 21501-4:2018. The values in Table 1 are acceptance limits, not target values.
| Parameter | Acceptance limit | Reference method |
|---|---|---|
| Sodium | ≤ 5 μg/L | ASTM D6800-18 ICP-MS |
| Potassium | ≤ 5 μg/L | ASTM D6800-18 ICP-MS |
| Calcium | ≤ 5 μg/L | ASTM D6800-18 ICP-MS |
| Magnesium | ≤ 5 μg/L | ASTM D6800-18 ICP-MS |
| Iron | ≤ 2 μg/L | ASTM D6800-18 ICP-MS |
| Copper | ≤ 2 μg/L | ASTM D6800-18 ICP-MS |
| Zinc | ≤ 2 μg/L | ASTM D6800-18 ICP-MS |
| Nickel | ≤ 2 μg/L | ASTM D6800-18 ICP-MS |
| Chromium | ≤ 2 μg/L | ASTM D6800-18 ICP-MS |
| Total cation burden | ≤ 30 μg/L | ASTM D6800-18 ICP-MS |
| Chloride | ≤ 200 μg/L | ASTM D4327-17 ion chromatography |
| Sulfate | ≤ 200 μg/L | ASTM D4327-17 ion chromatography |
| Particles ≥ 0.2 μm | ≤ 10 counts/mL | ISO 21501-4:2018 laser particle counting |
| Particles ≥ 0.5 μm | ≤ 2 counts/mL | ISO 21501-4:2018 laser particle counting |
| APHA color | < 5 | Visual comparison |
| Turbidity | < 0.3 NTU | ISO 7027-1:2016 nephlometric method |
Each container is blanketed with nitrogen during fill to reduce dissolved oxygen to <100 μg/L. The product is filtered through a 0.05 μm high-density polyethylene filter before packaging. All wetted components in the packaging train are selected to meet SEMI F57-0601 extraction limits.
Single-wafer spray processing uses a temperature-controlled dispense at 22 °C ± 0.5 °C and a spray flow of 0.8 L/min onto a 300 mm wafer rotating at 800 rpm for 60 s. The lower dispense temperature compensates for shorter chemical contact time in spray tools; etch uniformity across the wafer falls within 3% one-sigma for ALD AlOx films 10 nm thick. During the rinse sequence, ultrapure water is sprayed for 45 s and nitrogen purge at 25 L/min for 20 s prevents pattern collapse in high-aspect-ratio structures.
Thermal stability is the primary processing constraint. Qualification lot data show that aluminium-copper metal loss rises from 0.35 nm/min ± 0.05 nm/min at 30 °C to 0.8 nm/min ± 0.1 nm/min at 36 °C, while ALD AlOx loss increases only from 2.1 nm/min to 2.7 nm/min. The resulting AlOx-to-metal selectivity collapses from 6:1 to approximately 3.4:1. This nonlinear loss is attributed to destabilization of the aluminium passivation film and an increase in free-fluoride activity with temperature. The practical upper limit is therefore 35 °C for immersion baths; above 38 °C, the bath outgases more rapidly and bath life is shortened by 40%. Operation below 24 °C reduces throughput because the oxide removal rate falls below 1.1 nm/min.
Compared with 7:1 buffered oxide etch, the AOX-EC7 working bath contains lower free HF and a higher ammonium fluoride fraction; the free-fluoride electrode response is −385 mV versus Ag/AgCl at 25 °C, compared with −310 mV for 7:1 BOE. The consequence is reduced aluminium attack and lower via undercut in 0.35 μm and 0.18 μm pitch test structures. Against 0.5% dilute HF, AOX-EC7 incorporates a particle-dispersing surfactant that lowers organic residue re-deposition and improves post-rinse contact angle to ≤25° on aluminium-copper test coupons. Phosphoric acid-based aluminium etchants operate at 40 °C to 60 °C and remove both oxide and metal rapidly; they are unsuitable when only AlOx residue is targeted. Table 2 summarizes the comparative etch performance at nominal working conditions.
| Property | AOX-EC7 | BOE 7:1 | 0.5% DHF |
|---|---|---|---|
| Working pH at 25 °C | 2.9 ± 0.2 | 3.4 ± 0.2 | 2.3 ± 0.2 |
| ALD AlOx etch rate at 30 °C (nm/min) | 2.1 ± 0.3 | 4.5 ± 0.4 | 1.8 ± 0.3 |
| AlCu metal loss at 30 °C (nm/min) | 0.35 ± 0.05 | 2.0 ± 0.2 | 1.1 ± 0.1 |
| Selectivity ratio AlOx:AlCu | 6:1 | 2.2:1 | 1.6:1 |
| Recommended maximum bath temperature | 35 °C | 25 °C | 25 °C |
The formulation is incompatible with strong oxidizers, active metal powders, and concentrated acids. Bath containers must be PVDF, PFA, or fluoropolymer-lined HDPE; polypropylene and polycarbonate are unsuitable beyond 35 °C due to stress cracking. Waste neutralization requires fluoride precipitation with calcium hydroxide to pH 8.5–9.5 before discharge. The product must not be mixed with amine-based strippers because of exothermic neutralization and ammonium fluoride precipitation.