| HS Code | 242527 |
| Product Name | Ammonia-Hydrogen Peroxide Mixture (APM) Electronic/EL Grade |
| Chemical Formulation | NH4OH + H2O2 + H2O mixture |
| Appearance | Clear, colorless liquid |
| Physical State | Liquid at room temperature |
| Odor | Pungent, sharp ammonia-like odor |
| Ph | Approximately 10.5 to 11.5 (alkaline) |
| Specific Gravity | About 1.00 at 20°C |
| Boiling Point | Approximately 100°C with decomposition of hydrogen peroxide |
| Freezing Point | Approximately 0°C |
| Viscosity | About 1.0 cP at 20°C |
| Refractive Index | About 1.33 at 20°C |
| Vapor Pressure | About 23 hPa at 20°C |
| Solubility | Completely miscible with water |
As an accredited Ammonia-Hydrogen Peroxide Mixture (APM) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Each 4 L HDPE container sealed under nitrogen, packed in cleanroom-compatible double bags, ensures purity for electronic-grade APM. |
| Container Loading (20′ FCL) | 20′ FCL: sealed, compliant drums/IBCs of EL-grade APM loaded upright, blocked/braced, segregated from incompatible goods, with labels and spill containment secured. |
| Shipping | Ship as hazardous liquid, corrosive/oxidizer depending on concentration. Pack in sealed HDPE containers within UN-approved overpack. Maintain temperature below 40°C and protect from light. Segregate from acids, metals, and organic materials. Ensure secondary containment and proper labeling with relevant UN number and DOT/IMDG documentation for electronic-grade purity. |
| Storage | Store APM (Electronic/EL Grade) in tightly sealed HDPE or PTFE containers in a clean, cool, well-ventilated area away from heat, sunlight, acids, and organic materials. Keep segregated from incompatible substances and avoid metallic contamination. Maintain controlled temperature, regular leak checks, and proper labeling to ensure purity and prevent hazardous decomposition. |
| Shelf Life | Shelf life is typically short, usually 3-6 months from manufacture when stored tightly sealed in original container at recommended temperature. |
On 300 mm front-end-of-line logic and memory lines, post–chemical mechanical planarization wafers are transferred from a copper-barrier or oxide CMP unit to a wet bench configured with a PFA-lined overflow tank, bottom-fill nitrogen bubbling, and an in-line polytetrafluoroethylene 0.1 µm point-of-use filter. The APM solution is prepared by precision metering of 29% NH4OH and 31% H2O2 into ASTM D5127 Type E-1.2 ultrapure water at a volumetric ratio of 1:1:6. Bath temperature is held at 55 °C ± 1 °C. Megasonic energy at 925 kHz and 0.8 W/cm² is applied through a quartz transducer plate to remove ceria, colloidal silica, and organic slurry additives. The bath life after initial spiking is limited to 60 min; beyond this interval, H2O2 concentration decays from approximately 3.9% to below 3.0%, and ammonia loss shifts pH from 10.4 to 10.0. Light point defect counts on a KLA Surfscan SP5 set at 65 nm equivalent latex sphere resolution are typically held below 0.08 defects/cm² on monitor wafers. Finished wafers proceed to gate dielectric formation in FinFET or gate-all-around logic at nodes ≤ 5 nm, and to capacitor formation in DRAM or 3D NAND. Chemical inputs must be provided as SEMI C35 ammonium hydroxide and SEMI C30 hydrogen peroxide with Certificate of Analysis reporting Al, Ca, Cu, Fe, Ni, and Zn at or below 0.1 ppb. Exposed copper or cobalt films cannot be processed; the alkaline hydrogen peroxide mixture forms insoluble hydroxide precipitates above pH 9.0 that redeposit on the wafer surface. The mixture is also incompatible with chromium-bearing photomasks and with porous low-k dielectrics where alkaline solution uptake can shift k-value by more than 5%.
In shallow trench isolation post-CMP and sacrificial oxide strip integration, a dilute formulation of 1:1:50 NH4OH:H2O2:H2O at 40 °C is used as a soft particle lift-off step following oxide buffing. The reduced peroxide concentration limits chemical oxide growth on pad oxide and patterned active silicon to 0.3 nm over 90 s, measured by spectroscopic ellipsometry. Single-sided microroughness change on a 2 µm × 2 µm atomic force microscope scan remains below 0.12 nm RMS, compared with 0.45 nm RMS for conventional 1:1:5 at 70 °C. Sub-0.15 µm ceria particles are removed by electrostatic repulsion between the particle and the silicon oxide surface, both carrying zeta potentials more negative than -30 mV at pH 10.1. The bath is dispensed through a single-wafer spin processor with chilled chemical lines at 18 °C to limit ammonia evaporation. End products are embedded flash microcontrollers and automotive-grade logic wafers subject to AEC-Q100 reliability prequalification. Compliance is maintained under SEMI C35 and SEMI C30 incoming specifications, with particle loading in the fresh chemical below 0.5 counts/mL at a 0.1 µm analyzer threshold. The bath is not suitable for copper-exposed back-end-of-line structures because copper dissolution products can redeposit on dielectric surfaces.
Gen 8.5 organic light-emitting diode backplane fabrication uses APM spray and puddle treatment on 0.7 mm alkali-free glass before the first silicon oxide barrier deposition. The cleaning index is a water contact angle of less than 5° after 45 s of chemical exposure in a horizontal conveyorized chamber. The mixture ratio is 1:2:8 NH4OH:H2O2:H2O at 45 °C. It removes condensed organic films and organic residue from the glass substrate surface and reduces particle counts from 900 adders per m² to below 50 adders per m² at 0.3 µm inspection. Terminal products are 4K and 8K OLED panels as well as indium gallium zinc oxide thin-film transistor backplanes for high-refresh-rate LCDs. The incoming electronic-grade chemicals are monitored under SEMI C30 and SEMI C35. Waste ammonia from the process is neutralized before discharge under the European Union Industrial Emissions Directive 2010/75/EU where the fab falls within the scope of that directive. This step cannot be inserted after indium tin oxide sputtering because exposed ITO edges are attacked by the alkaline peroxide medium.
Monocrystalline p-type and n-type silicon wafers sawn with diamond wire are cleaned in a multi-stage immersion line where APM is dispensed at 1:2:7 NH4OH 29% : H2O2 31% : H2O at 60 °C for 180 s. The alkaline solution lifts silicon fines and water-soluble cutting fluid residues from the wafer surface and reduces the residual carbon signal measured by X-ray photoelectron spectroscopy to below 3 atomic %. Following the APM immersion, wafers enter a quick dump rinse and a hydrofluoric acid–ozone step before alkaline texturing in 2.5% KOH/isopropanol at 80 °C. The terminal finished products are M10 182 mm and G12 210 mm PERC, TOPCon, and heterojunction cells; for heterojunction, the APM step is positioned before intrinsic amorphous silicon deposition and after saw damage etch. Incoming hydrogen peroxide and ammonium hydroxide conform to SEMI C30 and SEMI C35. The process boundary is clear: APM cannot be used after screen-printed silver paste has been fired, because silver oxide formation and paste adhesion loss occur at pH above 10 and temperature above 50 °C.
In silicon epitaxial wafer production for insulated gate bipolar transistors and fast recovery diodes, a pre-clean sequence of APM at 1:1:5 and 60 °C for 120 s is inserted after hydrofluoric acid last-clean and before loading into the reduced-pressure chemical vapor deposition reactor. The APM step grows a sacrificial chemical oxide of 6–8 Å thickness, as measured by single-wavelength ellipsometry on a monitor wafer. This thin oxide volatilizes in the epitaxy chamber during pre-bake at 1,050 °C under hydrogen, removing surface carbon and oxygen in the same thermal cycle. The result is an epitaxial surface with stacking fault density below 0.1 cm⁻² after deposition. Chemical inputs are certified to SEMI C35 and SEMI C30; when available, wafer surface metal contamination before epitaxy is checked by total reflection X-ray fluorescence at a reporting limit of 1×1010 atoms/cm² for Fe, Ni, and Cu. The process is unsuitable for wafers with shallow implantation layers that would be oxidized by APM before activation. Published data for this specific configuration on heavily doped substrates below 8 Ω·cm is limited; qualification on the actual epitaxial reactor geometry is required.
Silicon carbide wafers entering gate oxidation after n-type drift region implantation and activation are treated with APM 1:1:5 at 70 °C for 10 min in a quartz carrier designed to avoid galvanic coupling between the wafer and silicon carbide process tool. The clean removes photoresist ash residue and adsorbed organic contamination without measurable attack on silicon-face or carbon-face surfaces; atomic force microscope roughness change on a 1 µm × 1 µm scan is below 0.05 nm RMS, within the repeatability limit of the metrology. This is followed by sacrificial oxide growth and etching to remove a 20–30 nm silicon carbide surface layer. Terminal devices are 650 V, 1,200 V, and 1,700 V SiC power MOSFETs and Schottky barrier diodes used in automotive on-board chargers and photovoltaic inverters. Incoming chemicals meet SEMI C35 and SEMI C30; the cleaning bay air cleanliness is ISO 14644-1:2015 Class 3. Exposure of nickel ohmic or copper top metallization to this APM condition is prohibited; at pH 10.2 and 70 °C, exposed copper forms oxide/hydroxide films and nickel undergoes ammonia complexation, leading to metal removal and contact degradation.
Through-silicon via forming for high-bandwidth memory uses a Bosch deep reactive ion etch followed by APM treatment at 1:1:10 and 50 °C for 60 s to remove fluoropolymer residue from the via sidewall before atomic layer deposition of the oxide liner. The wet process is run on a single-wafer cleaning tool that dispenses the solution into the via with a low-pressure nitrogen atomizer; this configuration prevents air bubble entrapment in vias of aspect ratio 10:1 or greater. Residual fluorine concentration on the via sidewall drops below 0.5 atomic %, as determined by time-of-flight secondary ion mass spectroscopy on a cleaved test vehicle. The terminal products are silicon interposers for 2.5D packaging and wafer-level stacked memory in mobile processors and AI accelerators. SEMI C35 and SEMI C30 grade chemicals are used. The process cannot be applied after copper barrier/seed deposition because the mixture dissolves copper and roughens the seed surface. Published data for through-silicon via diameter below 5 µm is limited.
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Ammonia-Hydrogen Peroxide Mixture (APM) Electronic/EL Grade is a point-of-use-blended aqueous cleaning chemistry composed of electronic-grade ammonium hydroxide, electronic-grade hydrogen peroxide, and ultrapure water. Representative commercial designations such as APM-EL-29/31 encode the raw-component assays: ammonium hydroxide supplied at 29.0% NH3 by weight and hydrogen peroxide supplied at 30–31% H2O2 by weight. The blend is prepared immediately before use at volumetric ratios from 1:1:5 to 1:2:10 (NH4OH:H2O2:H2O) to suppress pre-decomposition and ammonia loss. In semiconductor front-end wet processing, APM is the SC1 step of RCA cleaning, targeting particulate removal, organic film removal, and controlled silicon oxide regrowth. The bath operates in quartz or PFA immersion vessels at 60–80°C and a pH of 9.5–11.0. Mechanistically, H2O2 oxidizes the silicon surface, NH4OH undercuts adhered particles, and negative zeta potentials on both particle and substrate reduce re-adhesion.
Raw-component specifications for EL-grade APM are differentiated from technical-grade equivalents by trace impurity ceilings rather than assay shift. Supplier certificates of analysis for the NH4OH fraction typically report total critical metal impurities below 50 ppb, individual alkali and transition metals below 10 ppb, and chloride and sulfate below 500 ppb. The H2O2 fraction is specified at 30.0–31.0% with metal ceilings below 50 ppb, chloride below 500 ppb, and stabilizer-derived residue below 5 ppm. Blended APM is usually filtered through 0.1 μm PTFE or PFA membranes to maintain particle counts below 100 mL−1 at ≥0.2 μm. The ultrapure water fraction meets 18.2 MΩ·cm resistivity at 25°C, total organic carbon below 5 ppb, and dissolved oxygen below 10 ppb, with analytical controls following ASTM D5127-13 and ASTM D4327-17. Cation analyses are performed by ICP-MS with detection limits at or below 1 ppt; anion analysis uses suppressed ion chromatography.
Certificates of analysis for EL-grade APM components include lot-specific ICP-MS data for ≥20 elements, anion chromatograms, particle counts, and assay values traceable to NIST or equivalent reference materials. Solid residue after evaporation is specified because nonvolatile impurities concentrate at the wafer surface during drying. For NH4OH, residue after ignition is typically below 5 ppm; for H2O2, stabilizer residue is typically below 10 ppm. Incoming material is released against the supplier’s EL-grade internal specification, which is often aligned with SEMI C8 for ammonium hydroxide and SEMI C30 for hydrogen peroxide. In-line bath monitoring uses near-infrared H2O2 analyzers with accuracy of ±0.5% and conductivity or pH transmitters with accuracy of ±0.05 pH. Particle counts are measured by optical particle counters with 0.1 μm or 0.2 μm detection limits; a count exceeding 100 mL−1 triggers bath dump and filter replacement.
Bath lifetime in production SC1 systems is dominated by H2O2 decomposition and NH3 volatilization rather than by accumulation of removed residue. In open quartz overflow baths at 65°C, hydrogen peroxide half-life in mixed APM is typically 2–4 h; decomposition accelerates in the presence of transition-metal contamination, exposed heater surfaces, and megasonic energy. Ammonia evaporation reduces pH from an initial 10.3–10.8 toward 9.0 within one shift. When pH falls below 9.0, particle removal efficiency degrades because silica particles and the SiO2 surface lose negative zeta potential and re-adhesion increases. Point-of-use blending skids with conductometric or near-infrared bath analyzers maintain H2O2 by spiking when residual concentration falls below 70% of target and add NH4OH to restore pH. In batch immersion tools with recirculating filtration at 40–60 L·min−1 through 0.1 μm fluoropolymer cartridges, the bath is typically dumped after 4–8 h or 25 wafer batches, whichever occurs first. Megasonic transducers operating at 800–1,200 kHz and power densities of 5–15 W·cm−2 improve removal of sub-100 nm particles but shorten local peroxide lifetime near the transducer face. Power densities above 20 W·cm−2 have been associated with cavitation-induced damage on fragile gate stacks. Production failure modes include polypropylene filter housing stress cracking from alkaline exposure, quartz tank devitrification at pH above 11.5, and heater surface fouling from silicate precipitates when dissolved Si exceeds 10 ppm. Silicate precipitation is controlled by maintaining NH4OH concentration within ±5% of target and limiting bath temperature to 80°C.
EL-grade APM is technically distinct from acidic peroxide mixtures despite shared use of H2O2. APM is an alkaline oxidative cleaner that removes particulate and organic contamination by etching the interfacial oxide; it is not a metal-ion-removal chemistry and can redeposit dissolved metals if not followed by an acidic step. HPM (HCl/H2O2/H2O) at 1:1:6 to 1:2:8 and 65–80°C removes metallic contamination and alkali ions as soluble chloro complexes. SPM (H2SO4/H2O2) at 3:1 to 4:1 and 120–140°C strips heavy organic films and photoresist through peroxymonosulfuric acid oxidation but leaves sulfate residues and requires high-temperature quartz equipment. Dilute HF removes the final oxide but does not remove particulate; APM regrows a thin chemical oxide that must be removed separately in an HF/SC2 sequence. EL-grade APM also differs from commodity ammonia-peroxide blends in stabilizer control: electronic-grade H2O2 uses stabilizer packages that minimize Sn, Al, and phosphate residues and avoid adverse effects on gate oxide integrity. The product is therefore specified for front-end cleaning of 300 mm silicon and thin-film transistor substrates where trace metal contamination must remain below 1×1010 atoms·cm−2 on the wafer surface after cleaning.
| Mixture | Typical volumetric ratio | Operating temperature | Primary target residues | Critical limitation |
|---|---|---|---|---|
| APM (SC1) | NH4OH:H2O2:H2O = 1:1:5 to 1:2:10 | 60–80°C | Particles, organic surface films, interfacial oxide conditioning | Alkaline attack on low-κ films; NH3 loss and H2O2 decomposition limit bath life |
| HPM (SC2) | HCl:H2O2:H2O = 1:1:6 to 1:2:8 | 65–80°C | Metallic contamination, alkali ions | Chloride-induced corrosion of Cu and Ti |
| SPM | H2SO4:H2O2 = 3:1 to 4:1 | 120–140°C | Heavy organic films, photoresist strip | High viscosity, exotherm, sulfate residues |
In single-wafer spin tools, APM is dispensed at flow rates of 0.5–1.5 L·min−1 with heated PFA lines maintained at 60–80°C and purge times below 30 s to limit aerial ammonia. The blend is not suitable for removal of aluminum or silicon dioxide from contacts; its oxide etch component is small but non-zero, and process control often limits film loss per pass to below 0.5 nm on pre-gate oxide surfaces. APM must not be mixed with sulfuric acid, hydrochloric acid, or organic strippers in waste drains because exothermic neutralization releases oxygen and can generate hazardous gases. The bath is incompatible with unpassivated copper and cobalt surfaces and with porous low-κ dielectric films if pH exceeds 10.5. Carbon dioxide absorption from ambient air forms ammonium carbonate and increases particle counts; covered tanks and nitrogen blanketing at 0.1–0.3 L·min−1 are used to extend bath stability. For device structures with exposed TiN, TaN, or W, exposure time is restricted to 5 min or less at 60°C; published data for some cobalt and high-κ configurations are limited, so coupon testing is required before production release.
Surface organic removal by APM occurs through peroxide-generated radical species and ammonia-assisted dissolution, but the product is not designed to strip photoresist. For heavily implanted photoresist, SPM or plasma strip is required before APM treatment. The organic removal capability of APM is high for low-molecular-weight residues and fingerprints, but high-molecular-weight polymers may remain. Contact angle after APM cleaning on silicon is typically below 5°, indicating a hydrophilic surface. In flat-panel display and MEMS manufacturing, EL-grade APM is applied for glass cleaning and sacrificial oxide removal, but the low metal content is less critical than particle control. The mixture is used in immersion lines with ultrasonic or megasonic agitation; the presence of NH4OH can attack aluminum metallization at concentrations above 5%, so alternative etching routes are used for aluminum-containing substrates. Published data for specific display device configurations are limited; qualification is based on contact angle, surface roughness change, and trace metal deposition measured by total reflection X-ray fluorescence (TXRF).