| HS Code | 438562 |
| Chemical Formula | AsH₃ |
| Cas Number | 7784-42-1 |
| Grade | Electronic/EL Grade |
| Appearance | Colorless compressed liquefied gas |
| Odor | Faint garlic-like or fishy odor |
| Solubility In Water | Slightly soluble |
| Purity Min | 99.9999% |
| Molecular Symmetry | C3v |
As an accredited Arsine (AsH₃) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in seamless, high-pressure steel cylinders with safety valves and leak-tested seals. Available quantity: 47 liters (approximately 700 grams). |
| Container Loading (20′ FCL) | 20′ FCL: securely load Arsine gas cylinders upright, brace and label as toxic/dangerous, ensuring compliance and ventilation. |
| Shipping | Arsine (AsH₃) Electronic/EL Grade is shipped as a highly toxic, flammable liquefied compressed gas in DOT/UN-approved cylinders. Proper shipping name: Arsine, UN 2188, Hazard Class 2.3, Subsidiary 2.1. Transport requires poison-gas placards, secure ventilation, leak containment, and handling by trained hazmat professionals per regulations. |
| Storage | Store Arsine (AsH₃) Electronic/EL Grade as a liquefied gas in approved, secured, upright high-pressure cylinders in a cool, dry, well-ventilated area away from oxidizers and ignition sources. Use continuous leak detection, maintain cylinder valve protection, ground containers, and follow local hazardous-material codes. Ensure emergency shutdown and scrubber systems are available. |
| Shelf Life | Shelf life: typically 2 years from manufacture date when stored upright in a dry, cool, well-ventilated area. |
Gallium arsenide (GaAs) radio-frequency (RF) epitaxial growth with electronic-grade arsine functions as the primary arsenic supply for metal-organic chemical vapor deposition (MOCVD) of heterojunction bipolar transistors (HBTs) and pseudomorphic high-electron-mobility transistors (pHEMTs). In this downstream segment arsine is not blended into a polymer or paste formulation; it is diluted in palladium-diffused hydrogen and delivered through a pressure-regulated gas panel. The source cylinders are typically 5–10% AsH3 in hydrogen, and point-of-use dilution produces an arsine mole fraction of 0.5–2.0% at the reactor inlet. The V/III ratio, arsine molar flow divided by trimethylgallium plus trimethylaluminium molar flow, is maintained between 5–80. The compliance envelope includes ANSI/CGA G-13 for arsine handling, SEMI S2-0716 for equipment environmental, safety, and health risk minimization, and ISO 14644-1:2015 Class 5 or better for gas panel areas. Bulk purity of 99.9999% (6N) is specified on the certificate of analysis, with moisture and oxygen limits set by the purchaser and typically below 1 ppmv and 0.5 ppmv, respectively.
Downstream MOCVD reactors for GaAs RF are configured as multi-wafer planetary or turbodisc systems with capacities between 5×4-inch and 8×6-inch, operating at 50–100 Torr chamber pressure and 600–750 °C susceptor temperature. Arsine is delivered through dedicated group-V injector lines to prevent pre-reaction with trimethylgallium or trimethylaluminium. At susceptor temperatures above 600 °C, arsine is largely pyrolyzed to arsenic dimer/tetramer species and hydrogen; below approximately 500 °C, incomplete pyrolysis increases carbon incorporation from methyl radicals. The process sequence uses an arsine pre-flow of 5–15 s to establish an arsenic-stabilized surface on the GaAs substrate before group-III injection, and a post-growth arsine overpressure is maintained during cool-down until the wafer surface falls below 350–400 °C to suppress arsenic vacancy formation. In AlxGa1-xAs layers with x between 0.20 and 0.30, V/III is held in the upper portion of the range, 30–80, because the aluminium-containing surfaces are more sensitive to oxygen incorporation; low-carbon GaAs contact layers may use V/III of 5–20 to adjust carbon doping. Edge-to-center susceptor temperature non-uniformity is typically controlled within ±5 °C at a 700 °C setpoint; failure to maintain this band causes arsine cracking variability and sheet-resistance spread across the wafer.
Moisture ingress during cylinder change-out is the most common production-scale failure mode observed in this segment. If water contamination exceeds the cylinder specification, arsenic trioxide nucleation accumulates on mass flow controller internals, producing flow drift of more than 0.5% full scale and degrading epitaxial thickness uniformity; this is detected by in-situ reflectometry as deviation from the expected growth rate. Gas panel purge protocols of 50–100 system volumes with ultrapure nitrogen after cylinder replacement are therefore applied before reintroducing arsine to the reactor. Typical certificate-of-analysis limits for GaAs RF MOCVD also include CO, CO2, and total hydrocarbons below 0.5 ppmv and total metals below 10 ppbw; exceeding these limits has been correlated with increased base-emitter ideality factor in HBT epi wafers and reduced photoluminescence intensity. Terminal products from this segment are 100 mm and 150 mm epitaxial wafers populated with HBT or pHEMT layer stacks, which downstream fabs singulate into power amplifier, low-noise amplifier, RF switch, and front-end module die for mobile handsets, WiFi access points, and base-station phased-array transceivers. Finished die are qualified under JEDEC JESD22-A108D operating life testing and wafer acceptance criteria defined by the device manufacturer.
| Downstream stack | Susceptor temperature (°C) | Reactor pressure (Torr) | Arsine inlet mole fraction (%) | V/III or As/P ratio | Substrate diameter |
|---|---|---|---|---|---|
| GaAs RF HBT/pHEMT | 600–750 °C | 50–100 Torr | 0.5–2.0% | 5–80 | 100–150 mm |
| GaAs/AlGaAs VCSEL and IR LED | 680–780 °C | 50–150 Torr | 0.1–1.5% | 30–100 | 50–150 mm |
| InP photonic integrated circuits | 600–650 °C | 50–100 Torr | 0.2–2.0% | 10–60 V/III; 0.05–0.80 As/P | 50–100 mm |
| Ge/GaAs/InGaP multijunction solar | 650–750 °C | 60–100 Torr | 0.5–2.0% | 5–20 | 100–150 mm |
| InAs/GaSb Type-II superlattice | 450–520 °C | 50–100 Torr | 0.1–1.0% | 5–30 | 50–100 mm |
At mass-production GaAs/AlGaAs vertical-cavity surface-emitting laser fabs, the V/III ratio in the distributed Bragg reflector (DBR) structure is bounded by oxygen incorporation in high-aluminium AlxGa1-xAs on the low side and gas-phase pre-reaction on the high side. The supply gas is typically 10% AsH3 in hydrogen, diluted to 0.1–1.5 mol% at the reactor inlet. Total hydride flow is set to maintain V/III ratios of 30–100 for AlxGa1-xAs DBR layers with x between 0.85 and 0.95, and 10–40 for GaAs active regions and current-confinement layers. Compliance for this downstream segment includes ANSI/CGA G-13, SEMI S2-0716, ISO 14644-1:2015 Class 6 or better, and Telcordia GR-468-CORE for laser die reliability qualification.
Production MOCVD reactors for VCSEL epi use planetary multi-wafer configurations with capacities between 5×4-inch and 15×4-inch, operating at 50–150 Torr and 680–780 °C susceptor temperature. DBR stacks with 30–45 periods require long growth runs, and arsine flow stability over 4–8 h is critical. AlGaAs layers with high aluminium fraction are typically grown at V/III of 50–100 to suppress oxygen incorporation at aluminium sites; lower V/III leads to non-radiative recombination and laser threshold current drift. V/III above 100 tends to increase particulate formation through gas-phase reactions involving trimethylaluminium and arsine, producing coating drift on the susceptor and injector. The arsine flow is ramped with trimethylaluminium at DBR interfaces to maintain the specified ratio; if arsine flow lags during the aluminium-rich layer, oxygen-related defects increase and reflectance spectra degrade.
Batch-to-batch MFC drift above ±2% has been associated with DBR center-wavelength drift of ±1–2 nm on 850 nm VCSEL lots, requiring recalibration intervals of 6–12 months and reflectance mapping of calibration wafers. Terminal products include oxide-confined VCSELs at 850 nm and 940 nm for 3D sensing, LiDAR, optical data links, and industrial machine vision; high-speed infrared LEDs; and VCSEL arrays for proximity sensors. Finished devices in this segment are screened under Telcordia GR-468-CORE conditions and relevant JEDEC optoelectronic test methods defined by the end user.
Arsine enters ion implantation and diffusion doping as a dilute mixture of 1–10% in hydrogen, providing arsenic atoms for n-type junction formation in planar CMOS, discrete power, and image sensor flows. In beamline ion implanters, the mixture is supplied to a Bernas or Freeman ion source at 0.5–5 sccm arsine equivalent, with arc current of 0.5–5 A and extraction energy of 5–80 keV for source/drain and lightly doped drain implants. In atmospheric-pressure or low-pressure diffusion furnaces, arsine flow of 50–500 sccm with nitrogen or forming gas carrier in a 100–300-wafer vertical batch forms arsenic-doped polysilicon or drives arsenic into silicon at 850–1050 °C. The gas handling compliance envelope is ANSI/CGA G-13 and SEMI S2-0716, with point-of-use toxic gas monitors set to alarm at or below the 0.05 ppm OSHA 8-hour TWA.
The dominant operational boundary is arsenic deposition in the ion source. During extended arsine operation, arsenic accumulates on source insulators, causing beam instability and source failure after 100–200 hours for high-dose implants; production lines therefore use shut-off and inert purge cycles during idle periods. Post-implant annealing at 900–1050 °C with spike rapid thermal processing activates arsenic donors. Terminal products include n+ source/drain regions in CMOS logic and image sensor photodiode buried layers, as well as discrete power devices with arsenic-doped diffused regions. Published data for exact source lifetime varies by implanter manufacturer and source design.
Because the GaAs middle cell and InGaP top cell in a Ge/GaAs/InGaP triple-junction stack are grown by MOCVD, arsine-derived arsenic flux is the primary arsenic source for lattice-matched and strained layer processing on 100 mm or 150 mm germanium substrates. The reactor pressure is 60–100 Torr and growth temperature is 650–750 °C. Arsine is introduced at 0.5–2.0 mol% in hydrogen; the GaAs middle-cell V/III ratio is held between 5–20. For the InGaP top cell, arsine and phosphine are co-flowed with an As/P ratio selected to achieve an indium fraction near 0.49 and lattice mismatch below 0.1% relative to GaAs. The compliance framework includes ANSI/CGA G-13, SEMI S2-0716, and ASTM E490-00a(2019) for the AM0 reference spectrum used in cell I-V measurement.
Process control in this segment is dominated by the arsine pre-flow on germanium before III-V nucleation. An arsine pre-flow of 10–30 s at growth temperature passivates the Ge surface and stabilizes the nucleation layer against uncontrolled Ge/As intermixing. The GaAs middle cell is typically grown at 1.0–3.0 µm/h growth rate, and the InGaP top-cell growth rate is adjusted to maintain composition and ordering. Batch-to-batch drift in arsine mass flow of ±1% alters the InGaP As/P ratio enough to shift bandgap and current matching in the series-connected stack; production lots are therefore checked with external quantum efficiency mapping and current-voltage measurement under IEC 60904-3:2019. Terminal products include AM0 space solar cells with efficiencies near 30–32%, concentrated photovoltaic receiver cells rated for 500–1000 suns, and GaAs/InGaP dual-junction cells for terrestrial flat-plate photovoltaic modules.
Within InP-based photonic integrated circuit (PIC) manufacturing, arsine participates in lattice-matched In0.53Ga0.47As and InGaAsP layer growth for telecommunication laser and detector structures. The gas is delivered through a pressure-controlled run-vent manifold at 0.2–2.0 mol% in hydrogen. For In0.53Ga0.47As lattice-matched to InP, V/III ratio is 10–60; for InGaAsP quaternary layers covering 1.30–1.55 µm emission, the arsine-to-phosphine ratio is adjusted from 0.05–0.80 according to the target arsenic mole fraction. The compliance framework includes ANSI/CGA G-13, SEMI S2-0716, IEC 60825-1 for laser product safety, and Telcordia GR-468-CORE for optoelectronic reliability qualification.
Production MOCVD reactors for InP photonics are horizontal or showerhead systems with 7×2-inch to 5×4-inch capacity, operating at 50–100 Torr and 600–650 °C. The critical sequence is AsH3/PH3 switching at quantum-well and waveguide interfaces: a PH3 purge of 2–10 s after InGaAs growth reduces arsenic carryover into subsequent InP barriers, and an AsH3 pre-flow before InGaAsP growth restores the desired group-V surface coverage. Arsenic memory in the reactor and gas manifold can introduce unintentional As incorporation into InP cladding; in production distributed-feedback laser lots this is detected as photoluminescence broadening and threshold current drift when purge times are shortened below the reactor-specific minimum. In-line reflectance and curvature monitoring is used to track growth-rate drift and composition drift. Terminal products include 1310 nm and 1550 nm DFB laser chips, electro-absorption modulated lasers, semiconductor optical amplifiers, and waveguide-integrated photodetectors for 100G/400G/800G optical transceivers and coherent modules.
Growth of InAs/GaSb Type-II superlattice infrared absorber layers by MOCVD uses arsine as the arsenic precursor for InAs layers and trimethylantimony or trisdimethylaminoantimony as the antimony precursor for GaSb layers. This configuration is less industrialized than molecular beam epitaxy with solid arsenic crackers, and published data for this specific configuration is limited. In research and pilot MOCVD runs, arsine is diluted to 0.1–1.0 mol% in H2, and the V/III ratio for InAs layers is held between 5–30 to regulate arsenic incorporation while limiting gas-phase pre-reaction with trimethylindium. The GaSb layers are grown without arsine, so the group-V switch is arsine-to-antimony rather than arsenic-to-phosphorus. Compliance includes ANSI/CGA G-13, SEMI S2-0716, and ISO 14644-1:2015 Class 6 for MOCVD loading areas.
The process uses 450–520 °C susceptor temperature and 50–100 Torr reactor pressure, lower than GaAs or InP epitaxy because superlattice periods of 4–10 monolayers require abrupt interfaces and minimal interdiffusion. The arsine/antimony switching sequence consists of an AsH3 pre-flow before InAs, an H2 purge of 1–5 s, TMSb introduction for GaSb, and a further purge before the next InAs layer. Residual arsine in the gas panel contaminates the antimony surface and creates interface intermixing, which increases dark current in fabricated focal-plane arrays; low dead-leg injector designs and chamber bake-out procedures are used to manage this memory effect. Terminal product types include MWIR (3–5 µm) and LWIR (8–12 µm) focal-plane arrays for thermal imaging cameras, gas detection modules, and hyperspectral imaging systems; die-level screening is conducted to purchaser specification, often following MIL-STD-883J visual inspection methods.
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Arsine (AsH₃) Electronic/EL Grade is a semiconductor-purity liquefied gas supplied as the arsenic source for compound-semiconductor epitaxy, silicon n-type doping, and select optoelectronic fabrication routes. The product is certified to a minimum mole fraction of 99.9999% arsine, with trace impurity ceilings aligned to the SEMI C3 electronic-grade gas framework and verified lot-by-lot using gas chromatography with pulsed discharge helium ionization detection (GC-PDHID), cavity ring-down spectroscopy (CRDS), and gas-phase Fourier transform infrared spectroscopy (FTIR). The material carries CAS registry number 7784-42-1, UN transport number 2188, molecular mass 77.95 g mol⁻¹, boiling point −62.5 °C at 101.325 kPa, and gas density 2.695 g L⁻¹ at 0 °C and 101.325 kPa. The Electronic/EL Grade designation identifies an impurity specification rather than a cylinder model; packaged quantities are commonly 2.0 kg, 4.0 kg, and 10 kg net fill in 316L stainless steel or passivated carbon-steel cylinders. The distinction from technical-grade arsine is substantive: technical-grade material can contain O₂ and H₂O above 10 ppmv, while Electronic/EL Grade controls these oxide-forming impurities at or below 0.1 ppmv each.
| Parameter | Electronic/EL Grade Limit | Analytical Method | Reference Standard |
|---|---|---|---|
| Arsine purity | ≥ 99.9999 mol% | Mass balance / GC-PDHID | SEMI C3 |
| Oxygen (O₂) | ≤ 0.1 ppmv | GC-PDHID | SEMI C3 |
| Moisture (H₂O) | ≤ 0.1 ppmv | CRDS | SEMI C3 |
| Carbon monoxide (CO) | ≤ 0.1 ppmv | GC-PDHID | SEMI C3 |
| Carbon dioxide (CO₂) | ≤ 0.1 ppmv | GC-PDHID | SEMI C3 |
| Total hydrocarbons | ≤ 0.1 ppmv | GC-FID | SEMI C3 |
| Nitrogen (N₂) | ≤ 1 ppmv | GC-PDHID | SEMI C3 |
| Hydrogen (H₂) | ≤ 5 ppmv | GC-TCD | SEMI C3 |
| Phosphine (PH₃) | ≤ 0.5 ppmv | GC-FPD | SEMI C3 |
| Hydrogen sulfide (H₂S) | ≤ 0.01 ppmv | GC-FPD | SEMI C3 |
Analytical verification of Electronic/EL Grade arsine uses multi-method cross-checks to limit detector saturation and co-elution errors. Permanent gases are quantified by GC-PDHID on a molecular sieve column with cryogenic focusing; H₂S and PH₃ are quantified by gas chromatography with flame photometric detection at the 0.01 ppmv and 0.5 ppmv thresholds, respectively; moisture is measured by CRDS with a lower detection limit of approximately 0.02 ppmv. Particulate matter in the gas phase is controlled by in-line filtration with 0.003 µm stainless-steel filters at the fill manifold. Metal impurity data after impinger collection are reported as mass per gas volume and typically do not exceed 1 pg L⁻¹ for transition metals. Each cylinder is supplied with a certificate of analysis that includes fill site, cylinder number, and analytical equipment identification.
In production distribution, Electronic/EL Grade arsine is filled into dedicated vacuum-baked cylinders to reduce surface moisture and oxygen. Cylinders are prepared under a dry nitrogen inerting sequence with evacuation to 0.1 Pa and heated for 12–24 h at 80–120 °C. Internal surface roughness is specified at Ra ≤ 0.25 µm to limit particle shedding. Valve outlets conform to a CGA 350-type connection in North American distribution and equivalent ISO 5145-compatible valve outlet designations in international supply chains. Point-of-use delivery for electronic-grade arsine uses all-metal diaphragm regulators and orbital-welded 316L stainless steel tubing with helium leak-check rates below 1 × 10⁻⁹ Pa m³ s⁻¹. Dual-cylinder switchover panels and pressure transducers without exposed polymer components prevent pressure drop during multi-recipe MOCVD campaigns. Published data for this specific configuration is limited to facility-specific gas safety documentation; however, the key design requirement is the elimination of elastomer seals that can permeate moisture or adsorb arsine.
At the point of use, the critical difference between Electronic/EL Grade arsine and technical-grade arsine is not only bulk assay but the chemical form of trace impurities that participate in oxide inclusion and doping compensation. Technical-grade arsine is sold for metallurgy or reagent synthesis and may contain O₂ and H₂O above 10 ppmv, leading to arsenic oxide formation in gas lines and non-stoichiometric growth. Electronic/EL Grade arsine limits these species to ≤ 0.1 ppmv and adds tighter controls on sulfur compounds, which can act as shallow acceptors or surface passivators. Compared with phosphine (PH₃) in the same electronic gas family, arsine has a higher acute toxicity profile and lower delivery pressure at equivalent cylinder temperatures, requiring separate gas cabinet and sensor channels. Compared with liquid alternative arsenic sources such as tertiarybutylarsine (TBA), arsine is supplied as a high-pressure liquefied gas and provides a lower carbon background per arsenic atom during decomposition, but demands more rigorous exhaust and leak management. Electronic/EL Grade high-pressure arsine is also distinct from sub-atmospheric gas sources, where arsine is physically adsorbed onto a porous matrix. Sub-atmospheric sources reduce enclosure ventilation requirements and release volume during valve failure, but their maximum delivery rate is restricted by desorption kinetics and typically falls below the flow demand of multi-wafer MOCVD at 20 sccm. The high-pressure Electronic/EL Grade product is therefore used for processes requiring stable high flows, while sub-atmospheric packages are preferred for lower-throughput research tools.
| Attribute | Electronic/EL Grade AsH₃ | Technical-Grade AsH₃ | Tertiarybutylarsine (TBA) |
|---|---|---|---|
| Physical state at 25 °C | Liquefied gas | Liquefied gas | Liquid |
| Minimum purity | ≥ 99.9999 mol% | ≥ 99.5 mol% | Semiconductor liquid purity; carbon present |
| O₂ / H₂O limits | ≤ 0.1 ppmv each | Often > 10 ppmv | Not specified as gas impurity; carbon-bearing ligand |
| Primary use | MOCVD, ion implantation, diffusion | Metallurgy, reagent synthesis | Low-temperature MOCVD |
Application of Electronic/EL Grade arsine in metal-organic chemical vapor deposition (MOCVD) of GaAs, AlGaAs, and InGaAsP occurs in multi-wafer reactors with substrate temperatures of 550–750 °C, chamber pressures of 20–200 mbar, and AsH₃ flow rates of 1–20 sccm per wafer carrier. Arsine is introduced with trimethylgallium or trimethylindium through a temperature-controlled showerhead, and the group V/III ratio is maintained between 5:1 and 100:1. Thermal cracking of AsH₃ at the wafer surface releases arsenic species that incorporate into the growing layer; excess arsine is necessary to maintain a group V overpressure and suppress arsenic vacancy defects. At substrate temperatures below 550 °C, incomplete arsine decomposition lowers growth efficiency and increases hydrogen incorporation; above 700 °C, arsenic desorption generates surface roughness and increases the concentration of arsenic vacancies in the first monolayers. Process engineers monitor arsine-specific issues through mass flow controller (MFC) zero drift caused by arsenic mirror formation and through offline photoluminescence uniformity mapping. Optoelectronic processes for AlGaInP light-emitting diodes and InGaAs photodetectors use the same arsine delivery infrastructure; the key impurity constraint is H₂S at ≤ 0.01 ppmv because sulfur acts as a deep-level recombination center.
In silicon n-type doping, Electronic/EL Grade arsine is diluted to 10–1000 ppmv in hydrogen or nitrogen for diffusion furnace operation at 800–1050 °C. The gas is passed through a mass flow-controlled injector into the furnace, where arsenic reacts at the silicon surface and forms a doped glass; subsequent drive-in diffusion at 900–1100 °C determines junction depth. If moisture in the gas exceeds 0.1 ppmv, arsenic silicate glass thickness becomes non-uniform and sheet resistance variation across the wafer increases. For ion implantation, arsine is supplied in low-concentration mixtures, commonly 0.5–5% AsH₃ in H₂, to the ion source. Oxygen and moisture in the source gas accelerate filament oxidation and reduce beam current stability; the impurity ceilings of Electronic/EL Grade therefore correlate with longer ion source preventive maintenance intervals and lower As⁺ beam noise.
Because arsine is classified as acute toxic Category 1 under GHS and has an ACGIH TLV-TWA of 0.005 ppmv, cylinder changeout is performed only in forced-exhaust gas cabinets with exhaust velocity of at least 1.0 m s⁻¹. Continuous toxic gas detection is set to alarm at or below 0.005 ppmv and requires auto-isolation of the cylinder valve. Cylinder storage is limited to 40 °C and protected from oxidizers, halogens, nitric acid, and heat sources. In abatement, arsine is thermally oxidized or wet-scrubbed to arsenic oxides and arsenates; abatement efficiency of 99.9% is typical for integrated burn-box systems under manufacturer validation. The main operational failure mode in high-volume fabs is regulator and MFC drift caused by arsenic mirror deposition when moisture is introduced during cylinder changeout. Prevention requires purge cycles of 10–15 min with high-purity nitrogen and vacuum evacuation to below 0.1 Pa before reintroducing arsine. Published data for specific abatement units is limited to vendor test reports; however, the requirement for continuous effluent monitoring is contained in fab environmental permits.