| HS Code | 313359 |
| Product Name | Diborane (B2H6) Electronic/EL Grade |
| Chemical Name | Diborane |
| Cas Registry Number | 19287-45-7 |
| Molecular Formula | B2H6 |
| Molecular Weight | 27.67 g/mol |
| Purity | ≥99.999% (Electronic/EL Grade) |
| Physical State | Colorless gas at room temperature |
| Boiling Point | -92.5 °C |
| Melting Point | -165.5 °C |
| Relative Vapor Density | 0.95 (air = 1) |
| Lower Explosive Limit | 0.8% by volume in air |
| Autoignition Temperature | 38 °C |
| Reactivity With Water | Hydrolyzes, evolving hydrogen and forming boric acid |
| Un Number | UN 1911 |
As an accredited Diborane (B₂H₆) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in high-pressure steel cylinders (typically 20 kg), with CGA fittings and safety valves, for safe electronic-grade handling. |
| Container Loading (20′ FCL) | Load Diborane cylinders upright and secure in 20′ FCL, with proper ventilation and segregation from oxidizers. |
| Shipping | Diborane (B₂H₆) Electronic/EL Grade ships as a liquefied compressed gas in DOT-approved high-pressure cylinders, secured upright in ventilated containers. It requires strict hazardous material labeling, leak-proof connections, and ground transport only. Shipments comply with TIH/Hazmat regulations, avoiding heat, sparks, and incompatible oxidizers to ensure safe, contamination-free delivery. |
| Storage | Diborane (B₂H₆) Electronic/EL Grade must be stored as a compressed gas in secured, upright cylinders within a ventilated, explosion-proof gas cabinet. Keep the area cool, dry, and separated from oxidizers, moisture sources, and heat. Use continuous leak detection, corrosion-resistant fittings, and emergency shutoff systems. Ensure compliance with strict safety protocols for its pyrophoric and toxic nature. |
| Shelf Life | Diborane (B₂H₆) Electronic/EL Grade has a shelf life of 12 months when stored upright in a cool, dry, ventilated area. |
For in-situ boron-doped polysilicon films used in DRAM buried word lines and 3D-NAND gate stacks, electronic-grade diborane is delivered as a 1 vol% mixture in ultra-high-purity hydrogen or nitrogen. The gas originates from a SEMI C3.52-compliant cylinder cabinet with an all-stainless-steel panel, cross-purge sequencing, and a flow-restricting orifice rated for 10 sccm per cylinder. A horizontal hot-wall low-pressure chemical vapour deposition furnace with 150–200 wafer capacity and five-zone temperature control maintains 550–630 °C and 200–500 mTorr. Silane flow is set at 80–300 sccm, while diborane flow is ratioed to a gas-phase B:Si atomic ratio of 1×10⁻⁴ to 5×10⁻³. Deposition rate decreases from approximately 8 nm/min to 5 nm/min as diborane addition increases, because adsorbed boron species block silane adsorption sites. As-deposited resistivity falls between 1.2 mΩ·cm and 3.5 mΩ·cm at boron concentrations of 2×10¹⁹ atoms/cm³ to 8×10¹⁹ atoms/cm³, as measured by secondary ion mass spectrometry. Rapid thermal annealing at 900 °C for 30 s reduces resistivity to below 1.0 mΩ·cm through grain growth. Surface haze increases if B₂H₆ exceeds 0.5 vol% due to homogeneous nucleation in the stagnant boundary layer, which caps the maximum allowable diborane flow in this furnace design. Across-furnace sheet resistance variance of ±8% is observed due to source depletion; this is corrected by rebalancing left-right injector tubes and by injecting diborane only from the door side. Metallic contamination of Fe, Cu, and Ni is held below 1×10¹⁰ atoms/cm² by total reflection X-ray fluorescence, because iron at 10 ppb in the gas source increases DRAM junction leakage by several orders of magnitude.
The reflow integrity of borophosphosilicate glass deposited by sub-atmospheric chemical vapour deposition is governed by the B₂H₆-to-SiH₄ flow ratio, which controls B₂O₃ incorporation in the film. In a single-wafer SACVD chamber with faceplate temperature 180–200 °C, process pressure 200–700 Torr, and ozone injection, silane flow is fixed between 100 sccm and 500 sccm. Diborane is supplied as 1% in nitrogen at 50–300 sccm, and phosphine is supplied as 5% in nitrogen at 10–80 sccm. The resulting film contains 2–6 wt% boron and 2–8 wt% phosphorus, as measured by Fourier transform infrared spectroscopy using the B–O stretch near 1380 cm⁻¹ and the P=O stretch near 1320 cm⁻¹. Reflow at 850 °C in nitrogen produces step coverage of 85–90% on 0.5 µm features. Boron contents above 6 wt% cause post-reflow moisture uptake and B–O hydrolysis, which crystallizes the glass surface and initiates cracking during subsequent chemical mechanical planarisation. Deposition rate varies from 100 nm/min to 400 nm/min depending on ozone concentration and wafer temperature. Particle performance is monitored against ISO 14644-1 Class 4 in the transfer area. As-deposited stress is compressive at 100–300 MPa and relaxes below 50 MPa after reflow. The resulting doped glass is used as an interlayer dielectric in analogue mixed-signal and power management integrated circuits.
Inside a load-locked reduced-pressure chemical vapour deposition chamber with a lamp-heated single-wafer susceptor, selective SiGe epitaxy runs at 550–700 °C and 10–100 Torr. Dichlorosilane or silane supplies silicon, germane supplies germanium, and hydrogen chloride suppresses nucleation on oxide. Diborane is injected as 100 ppm in high-purity hydrogen at 5–100 sccm, producing boron concentrations from 2×10¹⁸ atoms/cm³ to 5×10²⁰ atoms/cm³. Chamber base pressure between wafers is held below 1×10⁻⁷ Torr. Boron incorporation is near-linear with diborane flow, but at flow above 60 sccm the selective window narrows because boron adsorption on oxide reduces HCl passivation efficiency. Growth rate is maintained at 10–50 nm/min, with the upper value restricted to the low-boron regime. The dominant process conflict is the memory effect: residual boron from the quartz liner and showerhead adds 3–5×10¹⁷ atoms/cm³ background doping if the chamber is not seasoned after wet clean. In-situ cleaning with remote NF₃ plasma is followed by a boron-doped silicon coat at 1×10¹⁹ atoms/cm³ to recondition the hardware. Emitter-base junction depth is controlled to 15–30 nm. These films form p-type base layers in SiGe heterojunction bipolar transistors for RF front-end modules and embedded SiGe in advanced CMOS.
Plasma doping of p-type source-drain extensions at the 28 nm and 14 nm logic nodes uses diborane-helium mixtures because a broad low-energy ion flux avoids the energy contamination inherent to BF₃ beamline implantation. A pulsed inductively coupled plasma source operating at 13.56 MHz with substrate bias from 100 V to 1000 V dissociates 1–5 vol% B₂H₆ in helium. Pulse widths are kept between 20 µs and 100 µs to limit deposition of boron-rich surface films. Retained boron dose is controlled between 5×10¹⁴ cm⁻² and 5×10¹⁵ cm⁻² after spike anneal, yielding junction depths below 10 nm. The main constraint is particulate boron generated by gas-phase nucleation when B₂H₆ exceeds 5% or RF power exceeds 3 kW. Exhaust particle counters trigger chamber dry clean when counts exceed 0.1 particles/cm³ at 0.1 µm detection threshold. Gas panel sequencing follows SEMI S2 exhaust monitoring and emergency shutdown protocols; diborane lines are double-contained and purged with helium after each lot. The resulting ultra-shallow junctions are integrated into FinFET and gate-all-around pMOS modules where dopant confinement within the first 10 nm of silicon is required for short-channel control.
To achieve boron nitride barrier films with sub-2% wafer uniformity, thermal atomic layer deposition alternates B₂H₆ and NH₃ pulses in a cross-flow reactor at 300–500 °C. The B₂H₆ pulse lasts 0.5–2 s, followed by an argon purge of 5–10 s, then an NH₃ pulse of 0.5–2 s and a second argon purge. Growth per cycle is 0.27–0.5 Å, and 200 mm wafer non-uniformity remains below 2% at 400 °C. X-ray photoelectron spectroscopy gives B:N atomic ratios of 1.0–1.1, with carbon and oxygen contamination below 1 at% after reactor preconditioning. The B₂H₆ and NH₃ lines remain physically segregated until the reaction zone because direct mixing forms solid Lewis acid-base adducts that clog the exhaust manifold. The resulting boron nitride films are used as moisture barriers in packaging and as dielectric spacers in advanced memory; published data for long-term reliability in copper interconnect integration remains limited.
Discrete power MOSFETs and insulated-gate bipolar transistors use a two-step boron predeposition and drive-in sequence when diborane is applied as the p-type dopant source. In predeposition, B₂H₆ is oxidised with dry oxygen at 400–600 °C in a quartz furnace, forming a borosilicate glass film on 150 mm or 200 mm silicon wafers. The B₂H₆ flow is 20–200 sccm of a 1% mixture, with the oxygen flow maintained at a 10:1 ratio above the diborane mixture to ensure complete oxidation. Borosilicate glass thickness is controlled from 50 nm to 200 nm. Drive-in is then performed at 1100–1250 °C for 2–10 h under nitrogen, yielding junction depths of 1–10 µm and surface concentrations of 1×10¹⁷–1×10¹⁹ atoms/cm³. The process constraint is thermal cycle time: each drive-in occupies the furnace for several hours and consumes 20–40 L/min of nitrogen. Boron depletion in the glass is monitored by four-point probe sheet resistance mapping after stripping the glass in dilute hydrofluoric acid. The resulting p-type junctions form the body diode anode and edge termination structures.
Competitive Diborane (B₂H₆) Electronic/EL Grade prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Intended for deposition and doping operations in semiconductor front-end manufacturing, Diborane (B2H6) Electronic/EL Grade is supplied as a purified, low-moisture boron source in high-pressure cylinder configurations. The compound has a molecular weight of 27.67 g mol-1, a normal boiling point of -92.5 °C, and a lower flammable limit in air of 0.8 vol%. Exposure control limits include an ACGIH TLV-TWA of 0.1 ppm and a NIOSH IDLH of 40 ppm. The Electronic/EL Grade is differentiated from industrial-grade diborane by internal cylinder surface passivation, dedicated high-purity filling lines, and lot-level analytical testing for volatile and metallic contaminants.
Reported certificates of analysis for Electronic/EL material typically specify total diborane purity at 99.999% (5N) or 99.995% where the mixture is certified on a hydrogen balance. The dominant volatile impurities are oxygen, nitrogen, methane, carbon monoxide, carbon dioxide, and water. Typical acceptance limits are 1 ppmv for O2, 2 ppmv for N2, 0.5 ppmv for CO, 0.5 ppmv for CO2, and 1 ppmv for H2O. Analytical methods include gas chromatography with pulsed discharge helium ionization for permanent gases, cavity ring-down spectroscopy or quartz crystal microbalance for moisture, and inductively coupled plasma mass spectrometry for Al, Fe, Cr, Ni, Cu, Na, and K. Particulate levels are controlled to 10 particles per ft3 at 0.1 µm or larger, aligned with semiconductor gas delivery specifications published by SEMI.
| Parameter | Typical Electronic/EL Grade Limit | Analytical Method |
|---|---|---|
| Total purity | 99.999% | GC-PDHID |
| Oxygen | <1 ppmv | GC-PDHID |
| Nitrogen | <2 ppmv | GC-PDHID |
| Carbon monoxide | <0.5 ppmv | GC-PDHID |
| Carbon dioxide | <0.5 ppmv | GC-PDHID |
| Moisture | <1 ppmv | CRDS or QCM |
| Total metals | <1 ppbw | ICP-MS |
| Particles | <10 ft-3 at 0.1 µm | Optical particle counter |
In low-pressure chemical vapor deposition of borosilicate glass and boron-doped polysilicon, the Electronic/EL Grade diborane is blended with silane and nitrous oxide or oxygen at chamber pressures between 50 mTorr and 300 mTorr and substrate temperatures from 550 °C to 700 °C. The boron incorporation efficiency depends on the diborane-to-silane flow ratio, typically 10-4 to 10-2. Because diborane decomposes at lower activation energy than boron trichloride, it enables p-type doping in polycrystalline silicon without requiring high-temperature H2 reduction. Residual water in the delivery line above 1 ppmv can hydrolyze diborane to boric acid, causing particle formation on the mass flow controller and chamber showerhead.
Ion implantation systems configured for diborane typically operate with source gas concentrations of 5 vol% or 10 vol% in hydrogen to balance ion source lifetime against beam current. The electron impact ionization of B2H6 produces B+ and B2H6+ fragments; compared with BF3, diborane avoids fluorine-associated cathode poisoning but requires hydrogen-compatible foreline and vacuum pump sealing surfaces. End-point detection and uniformity mapping on patterned wafers use sheet resistance ranges of 100 Ω/□ to 500 Ω/□ after rapid thermal annealing at 950 °C to 1050 °C.
Electronic/EL Grade diborane is packaged in high-pressure cylinders fabricated from 316L stainless steel with internal roughness below 25 Ra. Passivation procedures use repeated evacuation and low-concentration oxygen or nitrogen purge to create a stable oxide layer that minimizes diborane adsorption and hydrogen embrittlement. Cylinder valves are typically CGA 350 or DISS 632 with metal-to-metal seals; elastomeric seats are excluded because diborane is incompatible with many fluorocarbon elastomers at partial pressures above 50 kPa. Fill density is limited to 0.05 kg L-1 for pure diborane and lower for mixtures. Stored cylinders are held at temperatures below 40 °C to avoid thermal decomposition to hydrogen and higher boranes. Common product configurations include 5 vol% and 10 vol% hydrogen mixtures in 5 L, 25 L, and 49 L high-pressure cylinders. Model designations vary by gas supplier and are assigned to cylinder valve type, internal passivation protocol, and analytical lot size.
Delivery systems use gas cabinets with forced-exhaust velocity of 0.5 m s-1 minimum at the cabinet face and coaxial purging for valve manifold boxes. Abatement in compliance with local fire codes uses thermal oxidizers or water scrubbers followed by boron particulate filtration. Because diborane is pyrophoric, the use of oxygen exclusion, continuous leak detection, and open-flame exclusion devices is required in storage and distribution areas.
| Property/Parameter | Electronic/EL Grade Diborane | Industrial/Chemical Grade Diborane | BF3 Alternative Dopant |
|---|---|---|---|
| Typical total purity | 99.999% | 98–99.9% | 99.9% |
| Metal impurity control | <1 ppbw specified | Often unspecified | Often unspecified |
| Moisture specification | <1 ppmv | May exceed 10 ppmv | Varies by source |
| Primary application | CVD, plasma doping, and implantation | Organic synthesis reducing agent | Ion implantation |
| Packaging | Passivated 316L stainless steel | Carbon steel or unpurified stainless steel | Stainless steel |
| Typical mixture | 5–10 vol% in H2 | Pure or low-purity mixtures | Pure or mixed with inert gas |
Boron trichloride requires high-temperature hydrogen reduction, typically above 900 °C, to deposit boron in silicon; diborane decomposes at 300 °C to 400 °C, making it compatible with low-thermal-budget flows on advanced logic and DRAM devices. However, the diborane route introduces hydrogen and can shift silane-based deposition equilibrium; mass flow controllers with 0.01% setpoint precision and pressure-insensitive orifices are used to maintain the B:Si ratio. Published data on this specific configuration is limited for sub-7 nm nodes, especially for selective epitaxy where chalcogenide and carbon contamination must remain below 5 ppbw.
Operational boundaries include prohibition of diborane contact with oil-lubricated vacuum pumps, amine-based scrubbing agents, or halogenated cleaning solvents due to exothermic decomposition and toxic boron trioxide aerosol formation. Transfer lines must be heat-traced and moisture-purged to 1 ppmv before first gas introduction. When cylinders approach 0.5 MPa at delivery pressure, changeover procedures should divert to a fresh source to avoid concentration drift at the mass flow controller.