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Hydrogen Bromide (HBr) Electronic/EL Grade

    • Product Name: Hydrogen Bromide (HBr) Electronic/EL Grade
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 247187
    Chemical Name Hydrogen Bromide
    Chemical Formula HBr
    Cas Number 10035-10-6
    Molecular Weight 80.91 g/mol
    Grade Electronic/EL Grade
    Typical Purity ≥99.999%
    Appearance Colorless compressed liquefied gas; fumes in moist air
    Odor Sharp, pungent acrid odor
    Melting Point -86.82 °C
    Boiling Point -66.73 °C
    Vapor Pressure ~22 atm at 20 °C
    Gas Density 3.307 g/L at STP
    Liquid Density 1.49 g/mL at boiling point
    Solubility In Water Highly soluble; forms hydrobromic acid
    Flammability Non-flammable
    Corrosiveness Corrosive to skin, eyes, and metals

    As an accredited Hydrogen Bromide (HBr) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Hydrogen Bromide (HBr) Electronic/EL Grade is packaged as a high-purity compressed gas in passivated stainless steel cylinders, available in 20 kg quantities.
    Container Loading (20′ FCL) 20′ FCL loaded with Electronic Grade Hydrogen Bromide (HBr), secured as hazardous gas cylinders, per regulations, ready for transport.
    Shipping Hydrogen Bromide (HBr) Electronic/EL Grade is shipped as a liquefied, high-purity corrosive gas in specialized, moisture-free stainless steel or alloy cylinders with corrosion-resistant valves. Transportation requires strict compliance with DOT/IMDG/IATA regulations, including hazard class 2.3 (toxic gas) and 8 (corrosive) labeling, leak-proof seals, and secure upright handling to prevent exposure or contamination.
    Storage Hydrogen Bromide (HBr) Electronic/EL Grade must be stored in high-purity, corrosion-resistant cylinders or containers, kept tightly sealed in a cool, dry, well-ventilated area. Protect from moisture and direct sunlight. Isolate from oxidizers, bases, and reactive metals. Use appropriate leak detection and compatible materials; follow strict inventory control to maintain ultra-high purity and safety.
    Shelf Life Shelf life is typically 24 months from manufacture when stored in approved cylinders under cool, dry conditions, protected from moisture and contamination.
    Application of Hydrogen Bromide (HBr) Electronic/EL Grade

    In advanced logic and DRAM wafer fabrication, electronic-grade hydrogen bromide conforming to SEMI C3.52 is introduced into inductively coupled plasma etch chambers as the primary bromine radical source for polysilicon gate definition. The gas panel is constructed from 316L electropolished stainless steel with internal surface roughness below 0.25 µm Ra, orbitally welded joints, and helium leak rates below 1×10⁻⁹ mbar L s⁻¹; sub-fab gas cabinets are configured to SEMI S2-0200 hazardous gas requirements and monitored by SEMI S6 toxic gas detection. Typical mass-flow ratios are set at HBr:Cl₂ = 0.8:1 to 1.5:1, with total halogen flow between 80 sccm and 240 sccm, oxygen injection at 2–10 sccm, and helium dilution from 0 sccm to 100 sccm. Chamber pressure is maintained at 3–30 mTorr, dual-coil ICP source power at 600–1800 W, and cathode bias at 60–250 W, while electrostatic chuck temperature is controlled between 20 °C and 60 °C to avoid photoresist reticulation. Bromine radicals generated in the HBr/Cl₂ plasma adsorb on exposed silicon and desorb as volatile SiBrₓ etch products, whereas oxygen modulates a SiOₓBrᵧ sidewall passivation layer that suppresses lateral attack and limits critical dimension bias drift to below 1.5 nm across 300 mm wafers. Bulk polysilicon etch rates typically range from 250 nm min⁻¹ to 500 nm min⁻¹, and endpoint detection uses optical emission spectroscopy on SiBr and Br emission lines. Moisture ingress in HBr cylinder changeout is a documented production-scale failure mode: residual H₂O above 1 ppmv shifts the etch-to-deposition balance and increases chamber particle counts, so in-board point-of-use purifiers and 24 h line preconditioning are standard. The terminal finished product types include FinFET logic wafers, DRAM buried wordline structures, and 3D NAND stair-step polysilicon gates with gate lengths between 12 nm and 28 nm.

    What Limits the Mesa Sidewall Angle in InP-Based Laser Diodes When HBr/Cl₂/Ar Plasmas Are Used?

    The substitution of pure chlorine with an HBr/Cl₂/Ar mixture in inductively coupled plasma reactive ion etching of InP-based epilayers is governed by the balance between Br radical chemisorption and Ar⁺ sputtering. The HBr feed gas is delivered under SEMI C3.52 purity specifications, and wafer transfer occurs inside ISO 14644-1:2015 Class 5 cleanroom environments with loadport airflows maintained at ISO 14644-1:2015 Class 3 during cassette indexing. Gas mixing for InP/GaInAsP and InP/InGaAs structures typically uses HBr:Ar ratios from 1:1 to 4:1, chlorine addition between 5 vol% and 25 vol%, total flow from 20 sccm to 100 sccm, and chamber pressure between 1 mTorr and 10 mTorr. Source power is set at 500–1500 W and substrate bias at 50–250 W; helium backside cooling maintains wafer temperature at 30–80 °C. Under these conditions, Br radicals form InBr and PBr₃ desorption products, while Ar⁺ sputter removes nonvolatile In and P surface layers, producing mesa sidewall angles between 80° and 88° depending on the HBr:Ar ratio. Increasing HBr above 4:1 lowers etch rate below 0.2 µm min⁻¹ and deposits Br-rich polymer residue that requires post-etch HBr-based wet stripping; this is a known limitation when over-passivation is used to achieve vertical profiles. The terminal finished product types include distributed feedback laser diode bars, buried heterostructure lasers, waveguide photodiodes, and InP high electron mobility transistor wafers.

    Because FEOL post-etch residue removal requires a low-metal halogen acid that can be generated at the point of use, electronic-grade HBr is dissolved into ultrapure water to produce dilute hydrobromic acid for single-wafer cleaning after reactive ion etch. Ultrapure water quality conforms to ASTM D5127-13 Type E-1.2, the dissolution skid is fabricated from PFA and PTFE components, and the resulting acid is filtered through 0.05 µm PTFE cartridge filters immediately before the dispense nozzle. The standard blending ratio is 0.5–2.0 wt% HBr plus 0.1–0.8 wt% H₂O₂, with deionized water balance, heated to 25–60 °C in the process bowl. Contact time on a single-wafer spray tool is 30–120 s, and chamber exhaust is continuously monitored for bromine vapor while the drain is directed to acid neutralization. The HBr/H₂O₂ mixture lifts fluorinated organic residues from via sidewalls and removes titanium and tungsten halide byproducts without attacking low-k dielectric films when the HBr concentration remains below 2.5 wt%. Published data for residue-specific HBr cleaning formulations on porous low-k dielectrics is limited, so cassette-level etch-rate coupons are used to confirm dielectric loss below 0.3 nm min⁻¹ during process qualification. The terminal finished product is a cleaned FEOL wafer with light point defects below 30 counts wafer⁻¹ at 0.12 µm equivalent latex sphere threshold on darkfield inspection tools.

    ApplicationHBr-based formulationProcess windowPrimary complianceTerminal product
    Polysilicon gate etchHBr:Cl₂ = 0.8:11.5:1; O₂ 3–8 vol%3–30 mTorr; 20–60 °C; bias 60–250 WSEMI C3.52; SEMI S2-0200FinFET/DRAM wafers
    III-V mesa etchHBr:Ar = 1:14:1; Cl₂ 5–25 vol%1–10 mTorr; 30–80 °C; bias 50–250 WSEMI C3.52; ISO 14644-1:2015 Class 5Laser diodes, photodiodes
    Point-of-use HBr cleaning0.5–2.0 wt% HBr; 0.1–0.8 wt% H₂O₂25–60 °C; 30–120 s contactASTM D5127-13; SEMI C3.52FEOL cleaned wafers

    When Hydrogen-Bromine Flow Batteries Demand Sub-ppb Metal Impurity Electrolytes

    Containerized hydrogen-bromine flow battery systems use an aqueous bromide electrolyte prepared by absorbing electronic-grade HBr gas into chilled deionized water. The electrolyte loop is specified under IEC 62932-1:2018 for stationary flow battery safety and performance, and gas cylinders conform to UN 1048 for anhydrous hydrogen bromide transport with Class 2.3 toxic and Class 8 corrosive markings. The formulation target is 2–4 mol L⁻¹ hydrobromic acid with bromine loading between 0.5 mol L⁻¹ and 1.5 mol L⁻¹, maintained by an electrochemical bromine recovery loop rather than open chemical addition. Absorption is performed in a fluoropolymer-lined venturi scrubber with chilled water at 5–15 °C and a downstream heat exchanger that holds the electrolyte storage tank below 30 °C. Acrylonitrile butadiene styrene and polyvinyl chloride piping are not used in the electrolyte loop because bromine permeation causes embrittlement; fluoropolymer and graphite-filled polypropylene are specified downstream of the bromine injection point. The terminal finished product type is a 50 kW–2 MW flow battery stack integrated with hydrogen storage, fuel cell, and inverter modules for grid frequency regulation and solar load shifting. Published data for gas-derived hydrobromic acid purity limits in hydrogen-bromine flow batteries is limited, but system-level voltage efficiency loss above 0.5% per 100 cycles is a field-observed threshold when cation impurities are present.

    Methylammonium Bromide Precursor Synthesis Using Electronic-Grade HBr for Perovskite Photoactive Layers

    Synthesis of methylammonium bromide for lead-based and tin-based perovskite inks uses HBr gas as the acid source because the bromide counterion must not introduce residual sulfate, chloride, or metal impurities. The reaction vessel is a glass-lined stirred reactor with gas inlet sparger, operated under ISO 9001:2015 quality management and in compliance with REACH Regulation (EC) No 1907/2006 for downstream substance registration. HBr is metered into a methylamine solution in ethanol or 2-propanol at a 1.00:1 molar ratio, with reactor jacket temperature held at 0–20 °C to suppress methylamine loss and prevent thermal decomposition of the quaternary ammonium salt. Solids content at the end of addition is 30–45 wt%; the methylammonium bromide crystallizes by antisolvent addition of chilled methyl tert-butyl ether or toluene, then is vacuum dried at 60 °C and 10⁻² mbar for 12–24 h. The terminal finished product is a white crystalline powder with chloride content below 50 ppm and metal impurities below 5 ppm per metal by ICP-MS, used as a precursor in perovskite photovoltaic modules and X-ray detector devices.

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    Certification & Compliance
    More Introduction

    Hydrogen bromide, HBr, Electronic/EL Grade, is an anhydrous, liquefied halogenated gas supplied for plasma etch and wafer-cleaning chemistries in semiconductor fabrication. The Electronic/EL designation is a supplier-specific class rather than a universal model number; procurement documents should specify purity grade, cylinder water capacity, valve outlet, and certificate-of-analysis limits rather than relying on a vendor code alone. Commercial designations commonly include 5N HBr and 6N HBr, corresponding to minimum volumetric purities of 99.999 % and 99.9999 %, respectively. The anhydrous product is distinct from aqueous hydrobromic acid because free water in the feed gas destabilizes plasma uniformity and increases oxide defect density. Hydrogen bromide Electronic/EL Grade is used primarily where chlorine-based chemistry gives insufficient selectivity to silicon oxide or excessive photoresist consumption, especially in sub-10 nm node gate stack patterning and shallow trench isolation. Physical properties relevant to gas delivery include molecular mass 80.91 g/mol, boiling point -66.8 °C at 1.013 bar, CAS 10035-10-6, and UN 1048. At 20 °C, the liquefied gas exerts a vapor pressure in the approximate range 20–25 bar, which determines cylinder delivery pressure and gas cabinet temperature requirements.

    Why Does Point-of-Use HBr Purity Differ from the Cylinder Certificate?

    Point-of-use HBr purity is not guaranteed by the cylinder certificate alone. The gas is hygroscopic and attacks unpassivated metal surfaces in the presence of water; gas panels exposed to ambient air during cylinder replacement can release adsorbed moisture and particles into the process line. Production gas distribution system observations indicate that moisture spikes above 1.0 ppmv during first-gas sampling are most often caused by incomplete purge cycles or low purge gas flow rather than by a cylinder out-of-specification condition. High-integrity HBr gas cabinets use electropolished 316L stainless steel with surface roughness below 10 μin Ra, metal gasket seals, tied-diaphragm regulators, and point-of-use filters rated at 0.003 µm. Cylinder passivation with 5 % to 10 % HBr in nitrogen, followed by repeated pressurization and venting, is used to reduce adsorbed water and surface particulate before high-purity fill. Analytical methods for HBr include cavity ring-down spectroscopy for H₂O, gas chromatography with pulsed discharge ionization detection for permanent gases, and inductively coupled plasma mass spectrometry for trace metals; calibration and certificate issuance are maintained under ISO/IEC 17025:2017. Any valve or regulator replacement breaks the passivation envelope and must be followed by purge and moisture requalification before the gas panel is returned to process service.

    In gate stack patterning and shallow trench isolation etching, HBr-based plasmas are selected because bromine-containing etch products have lower volatility than chlorine-containing etch products at substrate temperatures below 120 °C. In an inductively coupled plasma process at pressure 5–25 mTorr, RF bias power 200–800 W, and total HBr/Cl₂/O₂ flow 100–400 sccm, silicon removal proceeds through ion-assisted desorption of SiBrₓ and SiClₓ, while SiO₂ remains partially passivated by the oxygen-containing plasma. Replacing part of the chlorine flow with HBr typically increases oxide selectivity and reduces undercut, but the process window narrows as HBr fraction increases because bromine-rich polymer deposits on chamber walls shift the etch/deposition balance. Chamber seasoning and wall temperature must therefore be specified in the process recipe. Anhydrous HBr is also distinguished from alternative bromine precursors such as BBr₃ and aqueous HBr. Boron tribromide is a liquid-source bromine precursor but introduces boron contamination, while aqueous hydrobromic acid cannot be admitted to a dry etch chamber without severe pressure instability and corrosion. Published data for a given film stack should be verified on the production tool; published data for this specific configuration is limited for the most advanced node films.

    Trace Metal Limits, Fill Environment, and Analytical Panel

    Electronic/EL Grade HBr is controlled at the ppt to ppb level for metals that degrade minority carrier lifetime and gate oxide integrity. Table 1 provides representative supplier specification ranges; the limits are not universal and must be checked against the vendor certificate of analysis. Cylinders are filled in cleanroom facilities meeting ISO 14644-1:2015 Class 5 or stricter, with particle counts verified by condensation particle counters. Fill lines are dedicated to HBr service and passivated to reduce iron, chromium, and nickel extraction. Batch-to-batch variance is controlled by homogenizing the HBr vapor before cylinder filling and by analyzing every lot for moisture, oxygen, nitrogen, carbon dioxide, total hydrocarbons, and the metal panel listed in Table 1. Nonvolatile residue methods after cylinder evacuation are also used for qualifying cylinder cleanliness for ULSI applications.

    Parameter5N Electronic Grade6N ULSI GradeAnalytical Method
    HBr purity≥ 99.999 % vol≥ 99.9999 % volGC-PDID or FTIR
    Water≤ 1.0 ppmv≤ 0.5 ppmvCRDS
    Oxygen≤ 1.0 ppmv≤ 0.5 ppmvGC-PDID
    Nitrogen≤ 5.0 ppmv≤ 1.0 ppmvGC-PDID
    Carbon dioxide≤ 1.0 ppmv≤ 0.5 ppmvFTIR
    Total hydrocarbons as CH₄≤ 1.0 ppmv≤ 0.1 ppmvGC-FID
    Metals, Fe, Cr, Ni, Na, K, Ca≤ 1.0 ppbw per element≤ 0.1 ppbw per elementICP-MS

    Technical-grade hydrogen bromide is not interchangeable with Electronic/EL Grade in front-end wafer processing. Technical anhydrous HBr may be supplied at 99.5 % or lower with water in the tens to hundreds ppmv range and no certified trace-metal panel. That moisture load hydrolyzes the gas in the delivery line and forms corrosive condensate; the resulting particle and metal contamination is sufficient to create gate oxide pinholes or shift threshold voltage. Electronic/EL Grade HBr also differs from hydrogen chloride and chlorine because the Si–Br etch product has a lower vapor pressure than SiCl₄ at substrate temperatures below 120 °C, enhancing sidewall passivation and increasing selectivity to SiO₂. Table 2 summarizes physical properties relevant to etch chamber design.

    PropertyHBrHClCl₂
    Molecular mass80.91 g/mol36.46 g/mol70.91 g/mol
    Boiling point at 1.013 bar-66.8 °C-85.1 °C-34.0 °C
    Etch product volatilityLower, promotes sidewall passivationHigh, promotes isotropic removalHigh, high etch rate
    Selectivity to SiO₂Typically higherLower without polymer additiveLow to moderate
    Metal compatibility riskCorrosive in moistureCorrosive in moistureStrong oxidizer

    When HBr Replaces Chlorine in High-Aspect-Ratio Silicon Etch

    Chlorine-based processes give high silicon etch rate but can lose profile control in features with aspect ratio above 30:1 because the etch product is volatile and sidewall passivation depends on added fluorocarbon or polymer precursors. Substituting 20 % to 60 % of the total halogen flow with HBr shifts the surface chemistry toward a bromine-dominated layer. The lower volatility of SiBrₓ reduces spontaneous chemical etching and increases the ion-energy dependence of the etch, enabling vertical sidewalls. However, the process window is sensitive to wall temperature and chamber seasoning; bromine-loaded chamber deposits can flake if wall temperature is not maintained above the deposition threshold. Production etch tools require periodic in-situ plasma clean with O₂ or NF₃ to remove Br-containing deposits, and the clean-step gas flow must be integrated into the process recipe to avoid etch rate drift. For advanced-node films, published data for this specific configuration is limited; process qualification should include etch rate, selectivity, and post-etch residue analysis on a patterned test wafer.

    Gas panel design for HBr service differs from HCl service because HBr has a higher boiling point and can condense in unheated low-pressure regions if the gas cabinet temperature is not controlled. Mass flow controllers are calibrated for HBr at 0–500 sccm or 0–1000 sccm full scale, and the control valve materials are selected for resistance to bromide corrosion. Point-of-use purifiers with 0.003 µm filtration are installed upstream of the mass flow controller; purifier cartridges must be replaced on a preventive maintenance schedule rather than on failure because metal scavenger capacity is not visible in line pressure. The gas distribution line is purged with high-purity nitrogen at 10–20 psig for a minimum of 10–15 min after cylinder replacement, followed by a low-flow HBr purge to passivate the regulator and valve seats. Flow stability is sensitive to cylinder pressure drop; low cylinder pressure can cause moisture enrichment in the vapor space and particle release from the cylinder wall.

    A Field-Relevant View of Impurity-Induced Gate Oxide Degradation

    Impurity effects are not linear. Moisture at 1.0 ppmv can produce hydroxyl-terminated surfaces that change etch selectivity, while transition metals at 1.0 ppbw can create mid-gap states if incorporated into gate dielectric. Batch-to-batch variation in HBr water content is therefore monitored with statistical process control and supplier change notification. A production line that switches from technical-grade to Electronic/EL Grade without changing the gas panel may observe persistent particle contamination because the delivery system remains coated with chlorides and oxides from the previous grade. The gas panel must be requalified after any pipe or regulator modification. Published data for impurity threshold values in specific gate stack materials is limited, so device fabricators typically establish internal lot acceptance limits that are tighter than the supplier specification and require a quarterly certificate of analysis with detail down to the 0.1 ppbw reporting level.

    Operational boundaries for Electronic/EL Grade HBr begin at cylinder changeout. The gas is toxic, corrosive, and incompatible with strong oxidizers, anhydrous ammonia, and elastomer-sealed components. Only metal-seated regulators and PCTFE or metal gaskets are used downstream of the cylinder. Dry HBr is compatible with electropolished 316L stainless steel, Hastelloy C-276, and Monel, but in the presence of moisture it attacks carbon steel, aluminum, and zinc. Gas cabinets are exhausted at a face velocity not less than 0.5 m/s and are leak-checked with a calibrated hazardous gas detector after each connection. Cylinder pressure decreases as the liquefied gas is withdrawn; Joule-Thomson cooling can reduce delivery pressure if the ambient temperature falls below 0 °C. The minimum stable cylinder pressure for a given mass flow should be determined on the production tool, and operation below that pressure is not recommended because moisture and volatile impurities concentrate in the vapor space. Equipment previously used for technical-grade HBr or HCl must not be placed into Electronic/EL Grade service without full passivation, particle flush, and analytical requalification.

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