| HS Code | 784109 |
| Chemical Formula | He |
| Cas Number | 7440-59-7 |
| Molecular Weight | 4.0026 g/mol |
| Purity | 99.9999% (6N) |
| State At 20 C | Gas |
| Boiling Point | -268.9 °C |
| Density | 0.1786 g/L at 0 °C, 1 atm |
| Critical Temperature | -267.96 °C |
| Critical Pressure | 2.24 atm |
| Solubility In Water | 0.00094 g/100 mL at 20 °C |
As an accredited Helium (He) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Helium (He) Electronic/EL Grade is supplied in a 49.5 L high-pressure gas cylinder, ensuring ultra-high purity for electronics manufacturing. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Helium EL Grade cylinders, secured upright, pressure-tested, labeled, ventilated, and shipment-ready for safe transport. |
| Shipping | Helium (He) Electronic/EL Grade is shipped as a non-flammable, non-toxic compressed gas under UN1963, Class 2.2. Packaged in high-pressure steel cylinders or tube trailers with valve protection. Store/secured upright, ventilated area. High-purity gas presents asphyxiation risk in confined spaces. Follow DOT/IATA requirements for labeling and transport. |
| Storage | Store Helium (Electronic/EL Grade) in secured, upright high-pressure cylinders in a cool, dry, well-ventilated area. Keep valves capped and protected; use appropriate regulators and leak-check connections. Avoid heat, ignition sources, and corrosive materials. Since it is an asphyxiant, ensure adequate ventilation and monitor oxygen levels. Follow manufacturer and safety data sheet guidelines. |
| Shelf Life | Shelf life is indefinite if cylinder and valve seals remain intact; helium is inert and stable, retaining purity. |
In plasma etch, physical vapor deposition, and ion implant tools, wafer temperature is controlled by helium introduced into the micro-gap between the wafer backside and the electrostatic chuck. Helium is used because its thermal conductivity at 10 Torr is markedly higher than nitrogen or argon at comparable pressure; this permits heat transfer across a non-contacting interface without introducing reactive species into the process environment. The gas is delivered as 100 vol% helium with purity specified to 99.9999 mol% under SEMI C3.39, and the facility distribution system is pressure-tested in accordance with ASME B31.3. The wafer-side leak rate is monitored by a capacitance manometer and a pressure-decay algorithm; if backside pressure rises beyond the tool setpoint, the process is interrupted to prevent wafer breakage.
The addition ratio in this application is not a formulated blend but a dual-zone pressure-throttling scheme. Center and edge zones are independently controlled; for a 300 mm etch chamber, center-zone pressure is commonly set between 2 Torr and 4 Torr, while edge-zone pressure is set between 6 Torr and 12 Torr, producing a center-to-edge ratio of approximately 1:2 to 1:3. Total helium flow into the chuck is typically 2–10 sccm; excessive flow raises chamber background pressure and shifts plasma impedance, whereas insufficient flow creates wafer hot spots at the edge. The pressure window is ±0.5 Torr for critical gate etch applications, beyond which wafer temperature non-uniformity degrades critical dimension uniformity. The production sequence includes wafer clamping, helium backfill, pressure stabilization, plasma processing, helium depressurization, and declamping. Failure modes observed on manufacturing lines include helium leakage through the wafer edge seal, polymer deposition inside chuck grooves, and particle trapping in backside gas microchannels. Terminal products include interlayer dielectric films, metal interconnects, gate structures, and passivation films on logic, memory, and power semiconductor wafers.
A silica optical fiber draw tower operates with a graphite resistance furnace heating the preform neck-down region above 2000 °C, after which the bare fiber must be cooled rapidly before primary coating application. Helium is injected through the cooling tube as a quench gas because its thermal conductivity at elevated temperature is higher than that of nitrogen or argon, allowing the fiber surface to reach a controlled temperature below the coating cure threshold within the available tower length. The helium is specified to electronic-grade purity of 99.9999 mol% under SEMI C3.39, and the draw tower environment is maintained in accordance with ISO 14644-1:2015. The addition ratio for this process is a volumetric flow condition: helium quench flow is typically 30–90 slpm through a 2 m cooling tube at draw speeds of 1500–2400 m/min. If helium is blended with argon to reduce cost, the helium fraction is maintained above 70 vol% to preserve the heat-transfer coefficient; below this threshold, fiber temperature at coating entry rises and primary coating concentricity deteriorates.
The production sequence begins with preform feed into the furnace, followed by bare-fiber diameter measurement, helium quenching, primary coating application, ultraviolet curing, fiber tension measurement, and winding onto shipping spools. Diameter control is maintained at 125±1 µm through continuous feedback to draw speed and furnace temperature. Helium supply interruption or pressure fluctuation shifts the cooling rate, producing transient diameter deviation and coating thickness defects; a buffer tank is therefore placed between the helium source and the draw tower mass flow controller. Terminal products include single-mode optical fiber meeting IEC 60793-2-50:2018 categories, multimode fiber, dispersion-shifted fiber, and fiber ribbon for telecommunication and data-center cabling.
A hermetic seal on a small-outline package is evaluated by helium fine leak testing to detect cavity leakage rates that would permit moisture ingress and internal corrosion over the device lifetime. Helium is used as the tracer gas because its small atomic radius and low atmospheric background allow detection of leak paths down to approximately 1×10⁻⁹ atm·cm³/s using a mass spectrometer leak detector. The applicable sequence is defined by MIL-STD-883 Method 1014 and JESD22-A109-B; the detector is calibrated to ASTM E498/E498M. Helium is introduced as 100 vol% tracer gas in the bombing chamber, not as a diluted formulation; the addition condition is therefore expressed as exposure pressure and dwell time rather than a blend ratio. For small cavity packages with internal volume below 0.01 cm³, the bombing pressure is typically 310–517 kPa and the dwell time is 2–4 h; after removal, the measured leak rate is compared against the reject limit derived from package volume and test condition under Method 1014. The production process includes pre-cleaning, helium bombing, evacuation, mass spectrometer leak detection, and accept/reject sorting; packages with gross leaks are first screened by fluorocarbon gross leak testing. Terminal products include hermetically sealed integrated circuit packages, MEMS inertial sensors, quartz crystal oscillators, and optoelectronic modules.
| Application | Helium introduction mode | Numerical range | Controlling standard |
|---|---|---|---|
| Plasma etch dilution | Gas mixture | 20–60 vol% He | SEMI C3.39 |
| Electrostatic chuck backside cooling | 100% He dual-zone pressure | center 2–4 Torr, edge 6–12 Torr | SEMI C3.39, ASME B31.3 |
| Optical fiber quench cooling | 100% He or He/Ar blend | 30–90 slpm, He ≥ 70 vol% | SEMI C3.39, IEC 60793-2-50:2018 |
| Hermetic package leak testing | 100% He tracer | 310–517 kPa, 2–4 h | MIL-STD-883 Method 1014, ASTM E498/E498M |
| Hard disk drive enclosure fill | 100% He fill gas | 0.9–1.0 atm absolute, O₂ ≤ 50 ppmv | ISO 14644-1:2015, SEMI C3.39 |
| MOCVD carrier gas | He/H₂/N₂ mixture | 20–50 vol% He of carrier flow | SEMI C3.39 |
The decision to fill a hard disk drive enclosure with helium is governed by aerodynamic behavior inside the head-disk assembly. Helium density is approximately one-seventh that of air, which reduces disk flutter, suspension vibration, and power consumption at the spindle motor; these effects permit narrower track spacing and higher platter counts within the same form factor. The fill gas is 100 vol% helium with purity not less than 99.99 mol% at lid seal, while oxygen is held below 50 ppmv and moisture below 10 ppmv to prevent oxidation of the head-media interface and lubricant degradation. Published data for this specific configuration is limited because drive manufacturers do not commonly release exact internal pressure and impurity specifications; however, the fill pressure is generally controlled at 0.9–1.0 atm absolute at the sealing event, with helium concentration verified by gas chromatography before weld closure. The production sequence includes head-disk assembly in an ISO 14644-1:2015 Class 5 cleanroom, servo track writing, helium injection through a fill port, lid seal laser welding, and post-seal leakage verification using ASTM E498/E498M or equivalent helium leak methods. A seal weld with porosity above the allowed threshold permits helium loss and air ingress, altering flying height and increasing the probability of head-disk contact. Terminal products include helium-filled high-capacity hard disk drives for data centers, surveillance storage, and network-attached storage systems.
During metalorganic chemical vapor deposition of gallium nitride-based light-emitting diode and laser diode structures, hydrogen carrier gas can incorporate into p-type GaN and form neutral Mg–H complexes that reduce effective acceptor concentration. Helium is introduced as an alternative carrier or dilution gas during p-GaN growth to reduce the hydrogen partial pressure in the reactor and improve post-growth Mg acceptor activation. The helium fraction is set by mass flow controllers at 20–50 vol% of total carrier flow, with total carrier flow for a multi-wafer reactor typically between 20 slm and 120 slm; the exact ratio is reactor-specific and is adjusted to maintain gas phase mixing without excessive pre-reaction of trimethylgallium and ammonia. The growth process is conducted at 900–1050 °C and 50–500 mbar chamber pressure, followed by post-growth annealing in nitrogen at 700–800 °C for 20–60 min to dissociate residual Mg–H complexes. Gas purity is specified under SEMI C3.39, and the epitaxial bay is maintained under ISO 14644-1:2015. Helium use is limited to p-GaN and indium-rich InGaN layers where hydrogen suppresses indium incorporation or Mg activation; use in n-GaN layers may not be economically justified because of helium supply cost and lower heat capacity relative to hydrogen. Terminal products include GaN-on-sapphire LED epitaxial wafers, blue and green laser diode structures, and GaN-based power electronic device epiwafers.
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Helium (He) Electronic/EL Grade is supplied in 50 L and 10 L water capacity cylinders manufactured to ISO 9809-1 with a nominal fill pressure of 200 bar at 20 °C. The product designation He-EL-5.5-200 identifies the electronic/EL grade, 5N5 minimum purity, and 200 bar fill configuration. Cylinder valve outlets are CGA 580 for North American delivery or DIN 6 for European installations. Cylinder preparation includes vacuum evacuation to below 1.0 × 10⁻¹ mbar, heated helium purge, and residual moisture check before filling. Each lot is homogenized for 24 h after filling and analyzed by gas chromatography with discharge ionization detection in accordance with ASTM D1945 and by cavity ring-down spectroscopy for moisture. The certificate of analysis reports cylinder serial number, fill lot, fill date, and measured impurities. The material is intended for semiconductor plasma etching, ion implantation purge, carrier gas in gas chromatography, and helium mass spectrometer leak detection where residual oxygen, moisture, or hydrocarbon levels would shift process windows or increase defect densities.
The distinction is not solely total purity. Industrial-grade helium at 99.995 % may contain oxygen and moisture levels that are acceptable for shielding gas but unacceptable for plasma chamber or detector use. UHP 99.999 % helium is common in analytical laboratories, but it may not carry the same cylinder preparation and packaging controls as electronic/EL material. The EL Grade designation adds a wafer-fab compatibility requirement: low-particulate packaging, restricted valve lubricants that could outgas volatile silicon species, and vacuum-based cylinder preparation before fill. In qualification, a lot is accepted at point-of-use only if total oxygen plus moisture is below 1.0 ppmv and total hydrocarbons are below 0.25 ppmv in the process gas line.
| Parameter | Limit | Analytical method |
|---|---|---|
| Helium purity | ≥ 99.9995 vol % | GC-DID, ASTM D1945 |
| Oxygen | ≤ 0.5 ppmv | GC-DID |
| Nitrogen | ≤ 1.0 ppmv | GC-DID |
| Moisture | ≤ 0.5 ppmv | Cavity ring-down spectroscopy |
| Total hydrocarbons as methane | ≤ 0.5 ppmv | GC-FID after catalytic conversion |
| Carbon monoxide plus carbon dioxide | ≤ 0.5 ppmv | GC-DID |
| Neon | ≤ 2.0 ppmv | GC-DID |
The specification is measured at the cylinder fill point. Point-of-use impurity levels depend on regulator purging, downstream filtration, and leak integrity. Electronic/EL Grade differs from standard UHP 5.0 helium in the lower moisture and hydrocarbon ceiling and in the cylinder vacuum preparation procedure. The hydrocarbon ceiling is relevant because carbonaceous deposits on plasma chamber electrodes and mass spectrometer ion sources can alter etch selectivity and detector baseline. Neon is controlled because neon contributes to residual gas analyzer baseline at mass 20 and can affect closed-loop semiconductor process monitoring.
On 300 mm plasma etch platforms, helium is introduced as a diluent at 50–200 sccm for fluorocarbon-based silicon dioxide and low-k dielectric etching. Chamber pressures are maintained at 10–50 mTorr with C4F8 or CF4 flow ratios of 5–20 sccm. The helium ionization potential is 24.59 eV; its lower mass relative to argon changes ion scattering and etch profile taper. Helium is also supplied to the electrostatic chuck backside at 4–10 Torr to couple wafer temperature to the chuck. The backside pressure is regulated with a manometer; an interlock is commonly set at 12 Torr to indicate chuck seal wear or wafer pop-up. Published data for this specific configuration is limited, but equipment maintenance logs associate helium pressure excursions with edge-cooling drift and polymer residue redistribution in high-aspect-ratio contact etch.
In PECVD of silicon dioxide using tetraethyl orthosilicate, helium carrier gas is passed through a heated ampoule at 60–80 °C with flow of 50–300 sccm. The helium stream must be free of moisture because TEOS hydrolysis in the delivery line forms polysiloxane deposits and particles larger than 0.5 µm. In medium-current ion implanters, helium is used as an inert purge for source housing and beamline components at 5–20 sccm; the gas does not generate dopant species and is pumped by turbomolecular pumps with base pressures below 1.0 × 10⁻⁶ Torr. Electronic/EL Grade is specified to avoid introducing water vapor, which is ionized to OH⁺ and can shorten ion source life.
Capillary gas chromatography with helium carrier at 1–2 mL/min depends on a stable column inlet pressure of 35–100 kPa. Residual oxygen at 0.5 ppmv or below reduces oxidative cleavage of polyethylene glycol stationary phases when the oven is held above 250 °C; published data for this specific configuration is limited, but stationary phase bleed increases as a function of oxygen exposure and temperature. For GC-MS, neon-bearing helium must be considered because the m/z 20 neon isotope contributes to baseline at mass 20 and can reduce detection limits for trace compounds with isobaric interferences. Electronic/EL Grade helium is therefore delivered with controlled neon and total hydrocarbon levels. Two-stage regulators with stainless steel or Hastelloy C-22 wetted parts are used; elastomeric seals are avoided because permeation can raise oxygen by 0.1–0.5 ppmv in a dead-headed regulator overnight. Thermal conductivity detector response is maintained with helium because the thermal conductivity difference between helium and most organic analytes is larger than for nitrogen; average linear velocity is typically set at 30–40 cm/s in 0.25 mm internal diameter columns.
| Grade | Typical purity | Oxygen | Moisture | Typical application |
|---|---|---|---|---|
| Industrial | 99.995 vol % | ≤ 5 ppmv | ≤ 5 ppmv | Shielding gas, noncritical purging |
| UHP 5.0 | 99.999 vol % | ≤ 1 ppmv | ≤ 1 ppmv | Analytical carrier, laboratory |
| Electronic/EL 5N5 | 99.9995 vol % | ≤ 0.5 ppmv | ≤ 0.5 ppmv | Semiconductor fab, GC-MS, leak detection |
| Research 6.0 | 99.9999 vol % | ≤ 0.1 ppmv | ≤ 0.1 ppmv | Epitaxy purge, cryogenic NMR |
The 50 L water capacity cylinder at 200 bar delivers approximately 10 m³ of gas at 20 °C and 1 atm; the 10 L cylinder delivers approximately 2 m³. Cylinder storage temperature range is −20 °C to 50 °C. Cylinders are restrained upright and segregated from oxidizers by 3 m or a 1 h fire-rated barrier in accordance with CGA P-1. Gas take-off is through a two-stage regulator with inlet rating 300 bar, outlet range 0–10 bar, and a leak rate below 1 × 10⁻⁹ mbar·L/s to prevent atmospheric back-diffusion when the cylinder is closed. CGA 580 and DIN 6 connections conform to ISO 5145 and are incompatible with oxidizing gas outlets, reducing cross-connection in manifold installations. Cylinder changeout requires purge of the regulator connection with 2–3 L/min helium for 30 s before process line isolation valves are opened. For semiconductor facilities, bulk helium is delivered through electro-polished 316L stainless steel orbital-welded lines with internal surface roughness below 0.25 µm Ra.
Helium mass spectrometer leak detection uses a calibrated leak standard of 1 × 10⁻⁹ Pa·m³/s to verify detector sensitivity. In hermetic package testing under MIL-STD-883 Method 1014, gross leak is performed after fine leak; the fine-leak criterion is often 5 × 10⁻⁸ mbar·L/s for cavity packages with volume below 0.01 cm³. Electronic/EL Grade helium prevents hydrocarbon contamination of the mass spectrometer ion source and avoids false background from tracer gas impurities. In refrigeration heat exchanger testing, helium leak rates of 1 × 10⁻⁶ mbar·L/s are acceptable for hermetically sealed compressor assemblies, while semiconductor valve-seat test standards may require 1 × 10⁻⁸ mbar·L/s. The cylinder pressure must be reduced to 1–3 bar at the detector inlet to avoid saturation of the turbomolecular pump and to maintain test-port pressure below 5 × 10⁻⁴ mbar.
High-flow purge of optoelectronic assembly benches is performed at 20–50 L/min through a point-of-use manifold to displace oxygen and moisture before laser diode soldering. The maximum safe working pressure at the manifold is 10 bar; direct connection to the 200 bar cylinder without pressure reduction is not permitted. Helium causes asphyxiation in unventilated enclosures; oxygen monitors set to alarm at 19.5 % O₂ are required per OSHA 29 CFR 1910.146 for confined-space entry. The product is not intended as a breathing gas and must not be used to inflate balloons or supply pneumatic tools without dew-point and oxygen compatibility review. Cryogenic helium transfer for superconducting applications is outside the EL Grade compressed-gas cylinder specification; liquid helium is covered separately by ISO 20421 and requires specialized vacuum-insulated transfer lines. Because helium has a low molecular mass, system leak rates are checked with a helium leak detector after manifold assembly; a background signal above 2 × 10⁻⁹ mbar·L/s indicates a fitting leak or purging error.