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Disilane (Si₂H₆) Electronic/EL Grade

    • Product Name: Disilane (Si₂H₆) 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 265343
    Chemical Name Disilane
    Chemical Formula Si2H6
    Product Grade Electronic/EL Grade
    Cas Number 1590-87-0
    Molecular Weight 62.22 g/mol
    Physical State At Stp Colorless gas
    Odor Acrid, pungent
    Melting Point -132.5 °C
    Boiling Point -14.5 °C
    Gas Density At Stp 2.78 g/L
    Relative Vapor Density 2.15 (air = 1)
    Solubility In Water Hydrolyzes/decomposes
    Flammability Pyrophoric in air
    Purity Level ≥99.999%

    As an accredited Disilane (Si₂H₆) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in a stainless steel high-pressure cylinder with CGA valve, net quantity 100 g, Electronic/EL grade disilane (Si₂H₆).
    Container Loading (20′ FCL) Load 20′ FCL with upright, secured Disilane cylinders; ensure ventilation, grounding, and proper hazard labeling for pyrophoric gas transport.
    Shipping Disilane (Si₂H₆), Electronic/EL Grade, ships as a pyrophoric, toxic, liquefied compressed gas in DOT-approved high-pressure cylinders. It requires upright, secured transport with protective valve caps, strict flammable-gas labeling, and segregation from oxidizers. Shipment is prohibited on passenger aircraft; handle only under inert atmosphere by trained personnel.
    Storage Disilane (Si₂H₆) Electronic/EL Grade is a pyrophoric, highly flammable gas. Store in approved, leak-tight high-pressure gas cylinders in a cool, dry, well-ventilated area or ventilated gas cabinet, secured upright. Isolate from oxidizers, ignition sources, and incompatible materials. Use only compatible regulators and equipment designed for pyrophoric gas service.
    Shelf Life Shelf life is typically 12 months when stored below 20°C in an approved cylinder, protected from moisture, heat, and ignition sources.
    Application of Disilane (Si₂H₆) Electronic/EL Grade

    In front-end logic manufacturing, the silicon nitride spacer and contact etch stop layer are deposited in hot-wall LPCVD furnaces where wafer thermal budget, pattern loading, and step coverage on three-dimensional gate structures constrain the choice of silicon precursor. Electronic-grade disilane is introduced through a dual-gauge stainless steel manifold after dilution to 5.0% in helium and is mixed with ammonia at a flow ratio of Si2H6:NH3 between 1:25 and 1:50. Deposition occurs at a total pressure of 0.3 Torr to 0.8 Torr and a substrate temperature of 550 °C to 650 °C, approximately 100 K to 150 K below the monosilane benchmark. In 300 mm batch furnaces, the lower thermal activation reduces the risk of transient enhanced diffusion in source/drain extensions, but it also shortens the mean residence time of the reactive gas front along the tube, requiring furnace zone temperatures to be trimmed by ±3 °C and pressure ramp rates limited to 0.1 Torr/min. The downstream production process is a batch LPCVD sequence: vertical or horizontal furnace boats holding 50 to 150 wafers are pre-heated under nitrogen, the disilane/ammonia gas mixture is injected through distributors, and an in-situ dry etch or purge step prevents powder accumulation on the tube walls. The silicon nitride film is used as a spacer and contact etch stop layer; the terminal product is a 300 mm logic or memory wafer at the front-end-of-line, before self-aligned contact metallization. Cleanroom compliance for wafer handling follows ISO 14644-1:2015 Class 3; gas delivery and abatement systems comply with SEMI S2 equipment safety guidelines and ANSI/ISA-84.00.01 for safety instrumented functions. Operational boundaries include an upper moisture limit of 1 ppmv in the helium dilution gas and a manifold purge requirement after each idle period exceeding 30 min; disilane must not be mixed with air or oxygen-containing lines because the material is pyrophoric at ambient temperature.

    What Limits Precursor Saturation in High-Aspect-Ratio 3D NAND Silicon Nitride Liners?

    Conformality loss in high-aspect-ratio 3D NAND dielectric liners is governed by precursor self-limiting adsorption on hydroxyl-terminated silicon oxide surfaces and by purge dynamics in structures with aspect ratios above 50:1. Disilane is used in plasma-enhanced atomic layer deposition processes as the silicon source for silicon nitride or silicon oxide liners because its lower decomposition threshold compared with monosilane enables saturation at substrate temperatures between 75 °C and 150 °C, where thermal decomposition of silane would be insufficient. In production-scale single-wafer ALD chambers, the precursor is delivered as a 5.0% mixture in helium through a heated line maintained above 60 °C to prevent condensation. The cycle sequence consists of a disilane pulse, an argon purge, an oxygen or nitrogen plasma step, and a second argon purge. Published data for disilane-specific PEALD on structures above 80:1 is limited; conformality below that threshold depends more on purge time than on precursor exposure dose.

    ParameterRepresentative rangeMeasurement or control method
    Si2H6 source concentration5.0% in Hemass flow controller with FTIR verification
    Substrate temperature75 °C to 150 °Cheated pedestal thermocouple array
    Argon purge step2 s to 10 spressure decay and downstream mass spectrometry
    Plasma power200 W to 500 W at 13.56 MHzRF impedance matching network
    Conformality on 50:1 aspect ratioabove 85%cross-section scanning electron microscopy

    In the PEALD silicon nitride liner process, the effective Si2H6:NH3 pulse flow ratio is maintained between 1:8 and 1:20, and the plasma step uses a nitrogen-argon mixture at a total pressure of 0.5 Torr to 2.0 Torr. The downstream production process is integrated into multi-step sequences for 3D NAND wordline liners and DRAM capacitor dielectric interface layers; the terminal products are memory wafers with silicon nitride liners in three-dimensional NAND arrays and silicon oxide interface liners in stacked capacitor DRAM cells. Device reliability qualification follows JEDEC JESD22-A108 for bias-temperature stress testing, while cleanroom control follows ISO 14644-1:2015 Class 3 and equipment safety compliance follows SEMI S2. An operational boundary is the requirement to purge the reactor for at least 5 s between precursor and plasma steps; insufficient purge produces gas-phase particles and non-uniform silicon incorporation in the form of silicon-rich films that shift etch rate and dielectric constant.

    Selective epitaxial growth of in situ boron-doped SiGe source/drain regions at the 3 nm node operates within a processing window where excessive wafer temperature causes germanium desorption and pattern loading, while insufficient temperature arrests crystalline growth on the exposed silicon surface. Disilane is delivered as a 1.0% mixture in hydrogen through a heated line to a single-wafer reduced-pressure chemical vapour deposition reactor; the gas ratio Si2H6:GeH4:HCl:H2 is typically maintained between 1:0.4:1.5:120 and 1:1.2:3.0:200 at a total pressure of 20 Torr to 80 Torr and a wafer temperature of 550 °C to 650 °C. The lower decomposition temperature of disilane compared with silane allows the process to avoid the 700 °C threshold at which boron diffusion and germanium surface segregation become difficult to control. Production-scale reactors require a separately controlled HCl etch step before the silicon source is introduced to remove native oxide from the recessed source/drain area; selectivity loss below 5 nm fin pitch is observed when the HCl flow ratio drops below 1.5, while excessive HCl causes facet erosion and silicon recess. The downstream process sequence is: recess etch, wet clean, pre-clean, selective SiGe epitaxy, in-situ boron doping, and post-epitaxial anneal. The terminal product is a FinFET or gate-all-around nanosheet wafer with fully strained SiGe source/drain regions before silicide contact formation. The manufacturing environment complies with ISO 14644-1:2015 Class 3; the epitaxy reactor and dopant gas delivery comply with SEMI S2, and reactor exhaust abatement is designed for hydrogen and hydrogen chloride mixtures. An operational boundary is the exclusion of oxygen above 10 ppbv in the hydrogen carrier gas, because silicon oxide formation at the growth interface produces stacking fault defects and increases contact resistance.

    Flexible OLED Thin-Film Encapsulation Silicon Nitride: Barrier Defect Density and Stress Control

    Barrier layer stacks in flexible organic light-emitting diode displays must maintain a water vapour transmission rate below 10−5 g/m²/day while bending through a radius of less than 2 mm without cracking. Disilane-based plasma-enhanced chemical vapour deposition is used to deposit silicon nitride at a substrate temperature of 80 °C to 120 °C, which is below the glass-transition limit of the polymer substrate and below the degradation threshold of the organic emissive layer. The gas feed ratio Si2H6:NH3:Ar is maintained between 1:8:40 and 1:15:60, with a total pressure of 0.5 Torr to 1.5 Torr and RF power density between 0.20 W/cm² and 0.45 W/cm² at 13.56 MHz. The production process is sheet-fed or roll-to-roll PECVD on polyimide carrier glass; barrier stacks alternate between silicon nitride and organic or inorganic planarisation layers to lengthen the diffusion path for water vapour and to interrupt pinhole propagation. The terminal product is a flexible OLED display panel with thin-film encapsulation, used in foldable mobile devices and automotive displays. Compliance includes ISO 14644-1:2015 Class 5 for display frontplane processing and IEC 62341-1 for OLED environmental test definitions. The process window is bounded by a sharp increase in compressive stress when RF power exceeds 0.45 W/cm²; this stress produces delamination at the polyimide interface after 10,000 bending cycles. Conversely, at power density below 0.20 W/cm², film density declines below 2.3 g/cm³ and the moisture barrier fails during damp-heat testing at 85 °C/85% relative humidity.

    When the Substrate Cannot Exceed 350°C: Disilane-Based Amorphous Silicon in TFT Backplanes

    Under 350 °C, the amorphous silicon channel layer deposited by plasma-enhanced chemical vapour deposition in thin-film transistor backplanes requires a precursor that undergoes sufficient gas-phase dissociation at reduced thermal input. Disilane is injected into a multi-chamber PECVD platform at a dilution of 5.0% to 10.0% in helium or hydrogen and combined with hydrogen at a Si2H6:H2 flow ratio of 1:20 to 1:50; deposition occurs at 250 °C to 350 °C, 1 Torr to 3 Torr, and RF power density between 0.05 W/cm² and 0.20 W/cm² at 13.56 MHz. The downstream process includes sequential deposition of gate dielectric, intrinsic amorphous silicon, n-type doped silicon, and source/drain metal on a glass substrate, followed by photolithography and reactive ion etching. The terminal product is a thin-film transistor backplane for LCD panels, organic light-emitting diode display pixel circuits, or medical X-ray flat panel detectors. Cleanroom compliance is ISO 14644-1:2015 Class 5; the PECVD system and gas cabinet comply with SEMI S2 and OSHA 29 CFR 1910.1200 hazard communication requirements. A process limitation appears when substrate temperature drops below 200 °C: hydrogen content in the amorphous silicon film rises above 15 at% and field-effect mobility falls below 0.5 cm²/Vs, making the backplane unsuitable for high-resolution displays. For disilane-specific mobility and threshold voltage stability data on large-area Gen 8.5 glass substrates, published data for this specific configuration is limited; equipment-specific characterisation is required before process transfer.

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    Certification & Compliance
    More Introduction

    Disilane (Si₂H₆) Electronic/EL Grade is a high-purity silicon precursor supplied as a liquefied compressed gas with a typical assay of 99.998% by volume (4N8) and, for advanced atomic layer deposition applications, 99.999% by volume (5N). Commercial model designations typically encode purity and application, such as DIS-EL-4N8 or an equivalent supplier code. The product is used in semiconductor front-end manufacturing for plasma-enhanced chemical vapor deposition, atomic layer deposition, and low-temperature epitaxial growth of silicon and silicon-germanium films. Its structural distinction from monosilane (SiH₄) is the direct silicon-silicon bond; this bond lowers the thermal decomposition onset and increases silicon atom delivery per mole of precursor. In manufacturing practice, that property allows disilane-based silicon nitride and silicon dioxide processes to operate at substrate temperatures up to 100–150 °C lower than comparable monosilane processes, reducing dopant diffusion in finFET and 3D NAND integration flows. The Electronic/EL Grade is specified for metal impurities in the parts-per-trillion by weight range and for oxygen, moisture, carbon-bearing species, and chlorosilanes at low parts-per-million or sub-parts-per-million levels. Cylinder configurations vary by supplier and commonly include electropolished 316L stainless steel bodies with flow-restrictor orifice valves for pyrophoric-gas service.

    What Differentiates Disilane from Monosilane in Low-Thermal-Budget Deposition?

    The primary kinetic distinction is the thermal decomposition pathway. Monosilane requires surface-mediated dissociation that becomes efficient at elevated temperatures, while disilane undergoes silicon-silicon bond homolysis and subsequent hydrogen elimination at lower energy. In 200 mm and 300 mm single-wafer plasma-enhanced chemical vapor deposition chambers, disilane has been used to deposit silicon nitride at 400 °C or below with ammonia and nitrogen plasma, whereas monosilane recipes targeting comparable film stress and density are commonly run at 400–600 °C depending on whether the reactor is PECVD or low-pressure chemical vapor deposition. The lower activation energy increases deposition rate per unit precursor flow, but it also narrows the gas-phase nucleation margin. Disilane-based processes therefore require tighter pressure and temperature ceilings because homogeneous nucleation can produce silicon particles that cause edge yield loss and showerhead fouling. In some single-wafer showerhead configurations, particle formation becomes significant above 5 Torr and 450 °C; however, published data for specific reactor geometries are limited, and equipment qualification on the target tool is required before process release.

    Representative Electronic/EL Grade release limits, aligned with the structure of SEMI C3.36 and typical supplier certificates, are shown in Table 1. The 5N column reflects higher-tier lots used in ALD and selective epitaxy where trace impurity incorporation has measurable impact on interface quality and film resistivity.

    Parameter4N8 Electronic Grade5N Electronic GradeAnalytical Method
    Purity99.998% by volume99.999% by volumeGC-PDHID, FTIR
    Silane (SiH₄)20 ppmv5 ppmvGC-PDHID
    Trisilane and higher silanes as Si₃H₈50 ppmv20 ppmvGC-PDHID
    Oxygen (O₂)1 ppmv0.5 ppmvGC-PDHID, electrochemical oxygen analyzer
    Moisture (H₂O)1 ppmv0.5 ppmvCRDS, FTIR
    Nitrogen (N₂)1 ppmv0.5 ppmvGC-PDHID
    Carbon monoxide (CO)1 ppmv0.5 ppmvGC-PDHID
    Carbon dioxide (CO₂)1 ppmv0.5 ppmvGC-PDHID
    Total hydrocarbons as methane1 ppmv0.5 ppmvGC-FID
    Chlorides as HCl1 ppmv0.5 ppmvIon chromatography
    Metals (Cr, Fe, Ni, Cu, Zn, Al, Ca, Na, K)1 ppbw each0.5 ppbw eachICP-MS
    Particles ≥ 0.1 µm2 particles/ft³1 particle/ft³Condensation particle counter

    Gas-phase impurity values are reported as volume fractions and metal values as weight fractions. Release testing is performed using gas chromatography with pulsed discharge helium ionization detection, Fourier-transform infrared spectroscopy, cavity ring-down spectroscopy, and inductively coupled plasma mass spectrometry. Particle counts are verified with condensation particle counters using compressed-gas sampling methodology derived from cleanroom measurement concepts in ISO 14644-1:2015.

    Low-Temperature Silicon Nitride and Silicon Epitaxy Process Boundaries

    Disilane is used in plasma-enhanced chemical vapor deposition of silicon nitride for gate sidewall spacers, etch stop layers, and stress liners where thermal budget after source-drain epitaxy is constrained. The molecule delivers two silicon atoms per precursor molecule, which reduces precursor flow demand and can improve conformality in high-aspect-ratio structures, but the same attribute increases mass loading per pulse in ALD. In plasma-assisted ALD of silicon nitride on 300 mm platforms, disilane pulse times of 0.5–2.0 seconds at 0.5–1.0 Torr are typical. Saturated growth per cycle is generally below 0.1 nm, although published data for specific reactor configurations vary with plasma power, electrode spacing, and substrate temperature. In low-temperature silicon epitaxy, disilane is introduced through heated injector paths with hydrogen carrier gas. Reported selective silicon growth processes for source/drain regions commonly operate between 500 °C and 650 °C, which is lower than many monosilane-based selective epitaxy processes in comparable reactor types. Process capability is strongly influenced by chamber pressure, hydrogen chloride co-flow, and pattern loading; qualification on patterned wafers is required because blanket-wafer deposition rate data do not predict selective growth behavior in high-aspect-ratio features.

    One production-scale limitation is gas-phase particle nucleation. In horizontal low-pressure chemical vapor deposition tube furnaces, disilane is rarely used below 300 °C because step coverage degrades from premature surface nucleation, while homogeneous nucleation becomes significant above 550 °C at pressures above 2 Torr in some tube configurations. These boundaries are not universal and must be mapped for each furnace geometry, wafer spacing, and precursor dilution level. Disilane also shifts film composition and silicon-to-nitrogen ratio at equal ammonia flow. No single flow ratio can be assigned without specifying RF power, electrode spacing, and total pressure; Rutherford backscattering spectrometry or X-ray photoelectron spectroscopy is used to confirm film stoichiometry during process development.

    Disilane is pyrophoric in air at room temperature. All distribution components must be constructed from electropolished 316L stainless steel with orbital welds and helium leak-tested to less than 1 × 10⁻⁹ mbar·L/s. Cylinder valves are fitted with flow-restrictor orifices, and gas cabinets are exhausted at a minimum face velocity of 200 ft/min (1.02 m/s). Moisture ingress must be held below 1 ppmv because hydrolysis produces siloxane oligomers and hydrogen, which can create pressure rise and contamination. Disilane is incompatible with oxidizers, halogens, and chlorinated cleaning agents. Exhaust streams are monitored with continuous flammable gas detectors calibrated for silane/disilane, with alarm setpoints at 25% of the lower flammability limit. Unlike dichlorosilane, disilane does not hydrolyze to chloride-rich residues, but its pyrophoricity imposes stricter handling protocols than dichlorosilane. Storage temperature should remain below 40 °C and away from localized heat sources. Cylinder outlet connections comply with CGA V-1 or regional equivalent for pyrophoric gas service.

    When Disilane Replaces Dichlorosilane in Chlorine-Sensitive Integration Flows

    Replacement of dichlorosilane with disilane is evaluated in silicon nitride and silicon epitaxy where chloride residues or hydrogen chloride formation create integration problems. Dichlorosilane-based low-pressure chemical vapor deposition silicon nitride at 700 °C produces hydrogen chloride as a byproduct; in high-aspect-ratio structures, hydrogen chloride can etch underlying features or combine with ammonia to form solid ammonium chloride particles. Disilane eliminates chlorine from the precursor and therefore removes chloride-induced corrosion and particulate defect modes. The trade-off is flammability: disilane is pyrophoric and requires stricter gas cabinet and exhaust management than dichlorosilane, which is flammable and corrosive but not pyrophoric. In nitride processes, disilane also allows deposition temperature reductions of roughly 100 °C relative to dichlorosilane at comparable pressure, though film stress and hydrogen content must be re-optimized. Table 2 compares selected properties relevant to precursor selection in silicon nitride and silicon epitaxy.

    AttributeDisilaneMonosilaneDichlorosilane
    Molar mass62.22 g/mol32.12 g/mol101.01 g/mol
    Boiling point at 1 atm-14.3 °C-111.9 °C8.2 °C
    Chlorine contentChlorine-freeChlorine-freeTwo chlorine atoms per molecule
    Pyrophoricity in airPyrophoricPyrophoricFlammable, not pyrophoric
    Relative deposition temperature at equal pressureLower than monosilaneBaselineHigher for some LPCVD processes
    Typical nitride chemistryLow-thermal-budget PECVD/ALDStandard PECVD/LPCVDLPCVD with HCl byproduct management
    Precursor cost and supplyHigher cost, smaller merchant volumeLower cost, high volumeLower cost, high volume

    For selective silicon epitaxy, disilane is used with hydrogen carrier gas and hydrogen chloride co-flow in the range 550–650 °C. Hydrogen chloride is retained as an etch-back species to achieve selectivity against oxide and nitride masks. Disilane provides a lower thermal path than dichlorosilane while avoiding chloride-rich residues, but its lower decomposition onset requires stricter control of injector temperature, chamber wall passivation, and gas residence time. Published data for specific integration stacks are limited; process qualification on patterned wafers is required for each device architecture.

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