| HS Code | 268234 |
| Product Name | DHF (Diluted Hydrofluoric Acid) with Surfactant |
| Grade | Electronic/EL Grade |
| Chemical Formula | HF + H2O + trace nonionic fluorosurfactant |
| Cas Number | 7664-39-3 (HF) |
| Concentration | Dilute HF; typical HF assay ranges from 0.1% to 5% |
| Appearance | Clear, colorless liquid |
| Odor | Pungent, sharp characteristic odor |
| Specific Gravity | 0.998 to 1.01 at 20°C depending on HF content |
| Refractive Index | 1.33 to 1.34 at 20°C |
| Ph | < 2 at 20°C |
| Boiling Point | Approximately 100°C at 1 atm for dilute aqueous HF |
| Freezing Point | Approximately 0°C for dilute aqueous HF |
| Metal Impurities | Each metal less than 1 ppb, including Al, Ca, Cu, Fe, K, Na and Zn |
| Particle Contamination | Less than 100 particles/mL at ≥ 0.5 μm |
| Surfactant Content | Proprietary low-residual nonionic fluorosurfactant, typically less than 10 ppm |
| Solubility | Fully miscible with water |
As an accredited DHF(With surfactant) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 4 L high-purity polyethylene bottles with nitrogen purge and tamper-evident seals, labeled Electronic/EL Grade DHF with surfactant. |
| Container Loading (20′ FCL) | 20' FCL: 20-foot container loaded with drummed/IBC-packed DHF (Electronic/EL Grade, with surfactant), secured per hazardous chemical regulations. |
| Shipping | Shipping description: **DHF (with surfactant) Electronic/EL Grade** is transported as **Dilute hydrofluoric acid solution, with surfactant**, **UN 1790**, **Hazard Class 8**, with subsidiary toxic risk, **Packing Group II**. Must be shipped in compatible polyethylene containers with proper corrosive/toxic labels, segregation, and emergency spill response documentation. |
| Storage | Store DHF (with surfactant) Electronic/EL Grade in tightly sealed, clearly labeled HDPE or PTFE containers. Keep in a cool, dry, well-ventilated chemical cabinet away from direct sunlight and incompatible materials. Use corrosion-resistant secondary containment, inspect regularly for leaks, and maintain stable temperatures. Ensure access is restricted to trained personnel. |
| Shelf Life | Shelf life is typically 6-12 months from manufacture date when stored sealed in original container under clean, temperature-controlled conditions. |
In front-end-of-line semiconductor wafer fabrication, the post-CMP and pre-diffusion cleaning sequence uses electronic/EL-grade dilute hydrofluoric acid formulated with a nonionic surfactant to remove oxide, metallic contamination, and slurry particles without breaching the device oxide-loss budget. The bath is prepared by blending 49 wt% electronic-grade HF with ultrapure water at a volumetric ratio between 1:100 and 1:200, producing a final HF concentration of 0.25–0.5 wt%; active surfactant is controlled at 200–500 ppm in immersion wet benches and at the lower endpoint in single-wafer spray tools to prevent foaming at the dispense nozzle. Applicable compliance requirements are SEMI S2 for exhaust and interlocks on the wet station, ASTM D5127-18 Type E-1.2 for dilution water, and ISO 14644-1:2015 Class 1–3 for the processing environment. In production, the solution is recirculated through a 0.05 µm PFA membrane filter, heated or cooled to 22–24 °C, and applied for 30–90 s in immersion mode or 20–60 s on a single-wafer spin processor. Rinsing in ultrapure water is followed by isopropyl alcohol-assisted Marangoni drying, which is specifically selected to prevent watermarks in high-aspect-ratio shallow trench isolation structures. Terminal device types associated with this application include logic microprocessors, DRAM, 3D NAND memory, and CMOS image sensors.
The critical process boundary is surfactant loading. At active surfactant concentrations above 500 ppm, the adsorbed monolayer on thermal oxide and TEOS surfaces can suppress the etch rate by 10–15% relative to the same HF concentration without surfactant; this reduction is typically measured by spectral ellipsometry on a 25 nm thermal oxide film before and after a timed immersion. At concentrations below 200 ppm, the bath surface tension remains above 50 mN/m, and the laser surface particle counter on 300 mm wafers shows incomplete removal of 0.1 µm silicon nitride particles. Batch-to-batch variation on 300 mm lines has been observed as a drift in post-rinse contact angle from 10° to 25° when surfactant depletion is not compensated, increasing wafer drying defects. The operational envelope is therefore maintained by periodic total organic carbon analysis and by setting upper and lower concentration alarms at ±15% around the qualified target. Published data for the exact etch-rate suppression coefficient of individual surfactant packages is limited and must be generated on the actual dielectric stack, because high-density plasma oxide and TEOS respond differently to surfactant adsorption than thermal oxide.
Flat-panel display wet stations employ dilute HF with a fluorosurfactant or polyoxyethylene-based surfactant for final glass cleaning before gate metal or gate insulator deposition. In a Gen 8.5 line handling 2200 mm × 2500 mm glass with thickness of 0.5–0.7 mm, the etchant is normally diluted from 49 wt% HF at 1:100 to 1:500, producing a final HF concentration of 0.1–0.5 wt%; surfactant active content is held between 50 ppm and 300 ppm. The process window is set by glass loss requirements: a 30–120 s contact time at 20–25 °C removes surface particles, alkali-earth metal contamination, and a thin altered layer without creating visible haze. Compliance is anchored to SEMI S2 for in-line equipment safety, SEMI F57 for wetted polymer extraction limits, and ISO 14644-1:2015 Class 5–7 zones depending on the position within the line. Downstream, the glass passes through a multiple-stage counter-current rinse, air-knife drying, and optical surface inspection before sputter or plasma-enhanced chemical vapor deposition. Terminal finished product types are TFT-LCD module panels and OLED backplane mother glass.
Over-etch control is the main processing conflict in this segment. If the conveyor speed is reduced or the HF concentration drifts above 0.5 wt%, glass removal can exceed 500 nm per pass; the resulting surface microroughness measured by atomic force microscopy can rise above 0.5 nm Ra, which shifts the subsequent gate dielectric uniformity. Conversely, concentrations below 0.1 wt% reduce particle removal efficiency and require longer megasonic exposure, increasing the risk of breakage on thin 0.5 mm glass. Therefore, the balance is not generic; it is specific to the glass composition and the thermal history of the incoming substrate.
Following alkaline texturing in monocrystalline PERC and TOPCon cell lines, the wafer surface carries residual silicate, metal contaminants, and chemical oxide that must be removed before tunnel-oxide or passivation-layer deposition. Surfactant-containing DHF is applied at a final HF concentration of 0.5–1.5 wt% and an active surfactant concentration of 50–200 ppm for 30–60 s at 20–25 °C. On multicrystalline acid texturing tools, a separate bath composed of 1–3 wt% HF, 5–15 wt% HNO₃, and 0.01–0.1 wt% surfactant at 6–12 °C is used to remove saw damage and generate an isotropic etch surface, with total silicon removal of 4–7 µm per side. The surfactant in this bath suppresses gas-bubble pinning at the reaction front; without it, localized etch-rate variation creates worm-mark defects and increases reflectance. Compliance requirements are SEMI S2 for tool safety, ASTM D5127-18 for water, and ISO 14644-1:2015 Class 6–8 for cell line cleaning environments. After the DHF step, wafers are rinsed in ultrapure water, dried, and transferred to diffusion or plasma-enhanced chemical vapor deposition. Terminal products include monocrystalline PERC cells, TOPCon cells, heterojunction cells, and assembled photovoltaic modules.
The process boundary most frequently encountered on production lines is the interaction between surfactant concentration and oxide removal rate on textured pyramids. Excess surfactant above 200 ppm can leave organic residue after rinse, which is detected as an increase in surface recombination or a contact angle above 10° after drying. In heterojunction lines, this residue is especially detrimental because it degrades the amorphous silicon passivation interface. On multicrystalline acid texturing lines, high surfactant loadings also reduce the etch depth per minute and shift the final wafer thickness; therefore, concentration is controlled by automated dosing with conductivity and density compensation. Published data for specific additive packages on industrial multicrystalline texturing baths is limited and is typically evaluated by pilot-scale etch depth, wafer reflectance, and minority carrier lifetime before full-line deployment.
| Application segment | Compliance anchor | Analytical verification | Typical control limit |
|---|---|---|---|
| Semiconductor front-end cleaning | SEMI S2; ASTM D5127-18 Type E-1.2; ISO 14644-1:2015 Class 1–3 | Laser surface particle counter, spectral ellipsometry | Oxide removal 1–3 nm per step; surfactant 200–500 ppm |
| FPD glass cleaning | SEMI S2; SEMI F57; ISO 14644-1:2015 Class 5–7 | Atomic force microscopy, contact angle, optical haze inspection | Glass removal ≤500 nm per pass; HF ≤0.5 wt% |
| Photovoltaic texturing and pre-passivation | SEMI S2; ASTM D5127-18; ISO 14644-1:2015 Class 6–8 | Reflectance mapping, minority carrier lifetime, thickness loss | Acid texture silicon removal 4–7 µm per side |
| MEMS sacrificial oxide release | SEMI S2; ISO 14644-1:2015 Class 5–7 | White-light interferometry, SEM stiction inspection | Final HF 2.3–8.2 wt%; surfactant 0.05–0.2 wt% |
| Compound semiconductor pre-epitaxial clean | SEMI S2; ASTM D5127-18; ISO 14644-1:2015 Class 4–6 | X-ray photoelectron spectroscopy, atomic force microscopy | HF 0.1–0.5 wt%; contact 15–60 s |
| Silicon test wafer reclaim | SEMI M1-0415; SEMI S2; ASTM D5127-18 | Surface particle counter, ellipsometry, thickness gage | Immersion 60–300 s; HF 0.5–1.0 wt% |
The sacrificial oxide release step in surface-micromachined MEMS processing removes silicon dioxide from beneath polysilicon beams and diaphragms, and the selection of a surfactant-containing DHF is driven by release-related stiction. A typical process uses 49 wt% HF diluted 1:5 to 1:20 by volume in ultrapure water, yielding final HF concentrations of 2.3–8.2 wt%; the surfactant active component is added at 0.05–0.2 wt% to lower the rinse liquid surface tension below 35 mN/m. The release etch is performed at 20–25 °C for 2–10 min, with the time determined by the sacrificial oxide thickness and the required lateral undercut. Compliance for the station includes SEMI S2 for HF fume extraction and drench shower interlocks, and ISO 14644-1:2015 Class 5–7 for cleanroom operations. After release, the wafer is transferred to a multi-cycle ultrapure water rinse, followed by surface-tension-gradient drying or supercritical CO₂ drying. Terminal finished product types include capacitive accelerometers, vibratory gyroscopes, pressure sensors, inkjet printheads, and RF MEMS switches.
The dominant process conflict is the trade-off between release rate and structural stiction. Higher HF concentrations above 8.2 wt% shorten the etch time but increase the etch-rate variability in constrained geometries; lower concentrations extend the etch and allow more water penetration into narrow gaps, increasing the probability of capillary adhesion. The surfactant mitigates this by reducing surface tension, but excessive surfactant loading above 0.2 wt% can deposit organic residue on released structures and shift resonant frequency after vacuum packaging. Moreover, this chemistry is not suitable for devices with exposed aluminum bond pads because fluoride-rich solutions attack aluminum; such designs require photoresist masking or the use of vapor HF. For CMOS-integrated MEMS wafers with back-end copper metallization, the process must be qualified through cross-section SEM and electrical test, because published data for the exact undercut rate in high-aspect-ratio oxide gaps is limited.
A pre-epitaxial wet-clean sequence in compound semiconductor MOCVD lines applies surfactant-containing DHF to remove surface oxides from GaAs and InP wafers and from GaN-on-sapphire templates before epitaxial growth. The final bath is typically maintained at 0.1–0.5 wt% HF with 50–200 ppm active surfactant, at 20–25 °C for 15–60 s in cassette immersion or single-wafer spin tools. On GaN-on-sapphire, the solution removes native gallium oxide and organic contamination without measurably roughening the sapphire substrate; on GaAs and InP, the short exposure window prevents selective loss of group V elements. Compliance is anchored to SEMI S2, ASTM D5127-18 water quality, and ISO 14644-1:2015 Class 4–6 cleanroom operation. The process continues with a 2–5 min ultrapure water overflow rinse, followed by nitrogen blow-off and immediate transfer to the load lock. Terminal products include LED epiwafers, laser diode epiwafers, RF power amplifiers on GaAs, and photodetectors on InP.
The limiting factor on compound semiconductor lines is the surface stoichiometry window. For InP substrates, exposure above 60 s or HF concentration above 0.5 wt% can increase surface roughness and alter the indium-to-phosphorus ratio, which is measured by X-ray photoelectron spectroscopy before and after cleaning. For GaAs, residual surfactant from an improperly rinsed cassette can introduce carbon at the epitaxial interface and reduce photoluminescence intensity. Therefore, the rinse is operated with overflow recycling and resistivity monitoring, with a final rinse water resistivity not less than 18.2 MΩ·cm at 25 °C. Published data for the exact effect of specific surfactant formulations on InP surface stoichiometry is limited; qualification on production epitaxial tools is required before a new surfactant package is released.
Wafer reclaim operations that convert used production wafers into monitor and test wafers use surfactant-containing DHF to strip thermal oxide, remove embedded metals, and lift slurry particles after photoresist removal and plasma ashing. The bath is formulated at 0.5–1.0 wt% HF with 100–300 ppm active surfactant, and immersion is maintained at 23 °C for 60–300 s depending on the incoming oxide thickness and the reclamation grade. Compliance requirements include SEMI M1-0415 for final wafer flatness, thickness, and surface particle criteria, SEMI S2 for the wet station, and ASTM D5127-18 for final rinse water. After the DHF etch, wafers receive brush scrubbing with dilute ammonium hydroxide, an RCA-type clean, HF-stripped final oxide, and laser particle inspection. The terminal product is a reclaimed bare silicon monitor wafer used in lithography, ion implantation, etch, and metrology equipment.
The operational boundary is repeated reclaim cycles. Each DHF step removes a finite silicon thickness, and after 3–5 reclaim cycles the wafer may approach the minimum thickness tolerance for the target monitor wafer specification; therefore, wafer thickness is measured after each cycle by capacitance gauge. The surfactant-modified DHF also has a defined capability limit: it does not remove copper that has diffused into the bulk silicon, and it cannot repair defect damage from prior process steps. For wafers with high levels of copper contamination, a gettering and polishing step must precede or follow the DHF etch. Published data for the exact etch selectivity to different implanted oxides on reclaimed wafers is limited, so reclaim lines validate incoming film stacks by Fourier-transform infrared spectroscopy before committing to the standard immersion time.
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DHF(With surfactant) Electronic/EL Grade is a dilute hydrofluoric acid cleaning formulation in which an electronic-grade hydrogen fluoride fraction is diluted with ultrapure water and blended with a nonionic surfactant package. The acid fraction is controlled to the cation and anion limits commonly associated with SEMI C29-0706 electronic-grade hydrofluoric acid. The resulting liquid is intended for oxide etching, native oxide removal, and particle removal on silicon and silicon dioxide surfaces in front-end semiconductor processing. The designation Electronic/EL Grade indicates that the product is filtered, assayed, and packaged under cleanroom-compatible conditions and is not a laboratory-grade or industrial-grade material.
Available process concentrations for the acid component are normally specified as a dilution band rather than a fixed product identity: common bands include 0.45–0.55 wt%, 0.95–1.05 wt%, and 4.5–5.5 wt% hydrogen fluoride. The surfactant concentration is application-defined, typically in the range 50–500 ppm, and is selected for low-foam behavior in recirculated wet benches. Because no single global standard fixes the surfactant identity, users should qualify the formulation against the specific etch rate and contact-angle response of the device flow, not against a generic dHF specification. The supplier specification sheet for this grade commonly encodes the hydrogen fluoride dilution and the surfactant addition; however, DHF(With surfactant) Electronic/EL Grade is not a universal fixed model number. Process-specific ordering codes are generated from the base dHF concentration, the surfactant loading, and the packaging size.
Addition of a nonionic surfactant reduces the air-liquid surface tension from the value for pure water, 72.8 mN/m at 25 °C, to a process envelope usually below 30 mN/m; some low-foam formulations stabilize between 25 mN/m and 28 mN/m when measured by forced-bubble tensiometry under ASTM D1331-20. The reduction in surface tension changes wetting behavior on hydrogen-terminated hydrophobic silicon after HF treatment. Sessile-drop contact-angle measurements on Si(100) with hydrogen termination are commonly reduced to below 10°, compared with values above 70° for surfactant-free dHF. This wetting shift is process-relevant because capillary penetration of high-aspect-ratio contact holes and trenches is governed by the capillary pressure relation Pcap = 2γ cosθ / r; a lower surface tension γ and lower contact angle θ reduce the driving pressure for pattern collapse during drying.
The surfactant also lowers the receding contact angle and inhibits droplet reattachment during spin-off, which affects watermark formation. However, the adsorbed surfactant layer can act as a transient barrier at the SiO2/HF interface. The initial etch rate may be suppressed by 10–20% in the first 5–10 s of immersion until the layer is disrupted or replenished. Process engineers should run an etch-rate verification wafer for each surfactant concentration and bath lifetime point, because published kinetic data for proprietary surfactant blends are limited.
In a batch immersion wet bench processing 300 mm wafers, the formulation is typically recirculated through 0.1 µm PTFE or PFA membrane filters at 22–25 °C. Wetted parts are fluoropolymer or high-purity polyethylene; borosilicate glass, stainless steel, and titanium fittings are incompatible with repeated HF contact. Bath turnover is usually set between 0.5 and 1.0 bath volumes per minute to keep surfactant homogeneously dispersed without excessive foaming. Foaming is the principal equipment failure mode observed on production recirculation systems when an unqualified surfactant package is used: foam can carry contaminants into the headspace and interfere with level sensors and overflow weirs.
Particle removal efficiency depends strongly on incoming wafer surface condition. Hydrofluoric acid without surfactant removes surface oxides but does not always reduce added particle counts on hydrophobic wafers because the high contact angle limits wetting and can leave particle-containing microlayer islands. With surfactant present, the liquid film spreads more uniformly, and particles are transported from the solid-liquid interface under the shear of recirculated flow or spin-off. Point-of-use particle monitoring is performed by laser light-scattering optical particle counters; typical electronic-grade release criteria for this product class are set at ≤25 counts/mL for particles ≥0.2 µm at the point of dispense, although this value is set by the user’s defect budget and not by a universal standard. The viscosity of the dilute formulation remains close to that of water at process temperature, commonly 0.9–1.1 mPa·s at 25 °C. Because surfactant addition is low, shear thinning is not significant in recirculation loops; pressure drop through fluoropolymer tubing is therefore dominated by line diameter and flow rate rather than by formulation rheology.
The product is defined by three analytical layers: hydrogen fluoride assay, surfactant concentration, and trace impurity profile. Hydrogen fluoride content is determined by acid-base titration or ion chromatography. Surfactant content is measured indirectly by surface tension and, in some laboratories, by LC-MS or evaporative light-scattering detection; the exact molecular identity may be proprietary. The trace-metal profile is controlled by ICP-MS with typical specification limits of ≤10 ppb for K, Na, Al, Fe, Cu, Ni, and Zn individually, and ≤100 ppb total trace metals in the highest-purity electronic-grade formulations. Anions such as chloride and sulfate are specified by ion chromatography; typical upper limits are ≤200 ppb for chloride and ≤500 ppb for sulfate, but these values are supplier-specific.
| Property | Representative range or limit | Analytical reference or method |
|---|---|---|
| Hydrogen fluoride content | 0.5–5.0 wt%, application-specific | Titration or ion chromatography; SEMI C29-0706 |
| Surfactant loading | 50–500 ppm, nonionic low-foam | Surface tension; LC-MS if required |
| Surface tension at 25 °C | 25–30 mN/m | ASTM D1331-20, forced-bubble tensiometer |
| Trace metal cations | ≤10 ppb each, ≤100 ppb total | ICP-MS; SEMI C29-0706 |
| Point-of-use particles | ≤25 counts/mL at ≥0.2 µm | Laser light-scattering particle counter; user-specified |
| Appearance | Clear, colorless liquid | Visual inspection |
The surfactant package must be selected from nonionic or weakly amphoteric chemistries. Anionic surfactants containing sodium or potassium counterions would compromise the trace-metal budget, while cationic surfactants can form complexes with fluoride and can adsorb too strongly on silicon dioxide. In production use, low-foam nonionic surfactants with cloud points above process temperature are preferred to avoid phase separation in heated baths. Batch-to-batch surface-tension variation should be controlled to within ±1 mN/m for stable wetting; larger variation can shift particle removal efficiency and etch uniformity.
In comparison with surfactant-free electronic-grade DHF and buffered oxide etchants, the primary discriminator is the surface-wetting behavior rather than the acid content alone. The following table summarizes the major separation points for process integration.
| Formulation | Surface tension at 25 °C | Thermal SiO2 etch behavior | Wetting of H-terminated Si | Key operational limitation |
|---|---|---|---|---|
| DHF with surfactant Electronic/EL Grade | 25–30 mN/m | Process-defined; for 1 wt% HF, commonly 100–300 Å/min | Contact angle <10° | Surfactant qualification and low-foam control required |
| Electronic-grade DHF without surfactant | ~72 mN/m | Similar base etch rate for equivalent HF concentration | Contact angle >70° | Poor wetting and particle removal on hydrophobic wafers |
| Buffered oxide etch 7:1 | ~72 mN/m | 800–1200 Å/min for thermal SiO2 at 25 °C | Contact angle high | Ammonium fluoride residue risk; higher pH may alter surface charge |
For thermal SiO2 films grown at 900–1000 °C in dry oxygen, dilute HF etching proceeds by fluoride attack on the oxide network. The etch rate depends on HF concentration, temperature, oxide density, surfactant adsorption, and bath mass transport. In stirred baths at 25 °C, a 1 wt% HF solution without surfactant typically removes thermal oxide at 100–300 Å/min. The surfactant-containing formulation may show an initial lag and then converge to within 10–20% of the surfactant-free rate, but the value must be confirmed on the specific thermal oxide thickness and tool configuration. Dense thermal oxides etch more slowly than wet chemical oxides or low-temperature CVD oxides; the formulation cannot be expected to produce the same rate across all oxide types.
In single-wafer spin processors, improved wetting creates a more uniform liquid meniscus during dispense and spin-off. Dispense volumes of 1.0–1.5 L/min through fluoropolymer nozzles, with spin speeds from 100–500 rpm during chemical dwell and 800–1500 rpm during rinse and dry, are representative of production recipes but are tool-specific. The reduction in surface tension from 72 mN/m to 30 mN/m or lower directly reduces capillary stress on high-aspect-ratio patterns. For a cylindrical feature of radius 100 nm, the capillary pressure estimate 2γ/r gives approximately 1.5 MPa for water-like surface tension and 0.6 MPa for the surfactant-modified formulation. Contact-angle hysteresis and feature geometry must be included for a quantitative pattern-collapse model, and published data for this specific surfactant configuration is limited.
For post-etch rinsing, the wafer surface must be transferred to ultrapure water before the hydrophobic surface dries unevenly. In single-wafer tools, an overflow rinse with ultrapure water is followed by spin dry; in batch tools, an overflow rinse bath or quick dump rinse is used. Surfactant can alter rinse time because residual surfactant desorbs slowly from silicon dioxide and hydrogen-terminated silicon. Rinse resistance is monitored by surface tension of the final rinse water or by total organic carbon; a typical point-of-use total organic carbon limit is ≤10 ppb in the final rinse, but this is not a release criterion for the chemical itself. Incomplete surfactant removal can leave organic residue after dry and influence subsequent gate dielectric deposition.
Operational limitations are defined by the chemistry and by the packaging system. The formulation must not be stored in glass or metal containers; PFA, PTFE, or high-density polyethylene are acceptable. Storage above 40 °C increases HF vapor pressure and may degrade the surfactant; storage below 0 °C may cause phase separation or freezing. The product must not be mixed with strong alkalis, ammonia, or oxidizers such as nitric acid unless the target process has been qualified, because exothermic neutralization or toxic gas release can occur. Local exhaust with HF scrubbing and conductivity-based leak detection are standard engineering controls. Mixing with amine-based additives should be avoided because amine-HF salt formation can alter free fluoride availability and produce uncontrolled heat release at point-of-use.