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Gold Plating Salt (BASF Electronic Grade Gold Salt) Electronic/EL Grade

    • Product Name: Gold Plating Salt (BASF Electronic Grade Gold Salt) 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 597849
    Product Name Gold Plating Salt (BASF Electronic Grade Gold Salt) Electronic/EL Grade
    Chemical Name Potassium dicyanoaurate(I)
    Cas Number 13967-50-5
    Molecular Formula KAu(CN)2
    Molecular Weight 288.10 g/mol
    Gold Content 68.2% minimum
    Purity 99.9% minimum (Electronic/EL Grade)
    Appearance White crystalline powder
    Solubility In Water Soluble in water
    Ph Of 1 Aqueous Solution 6.0 to 8.0
    Bulk Density Approximately 0.9 g/cm3
    Moisture Content 0.5% maximum
    Water Insoluble Matter 0.1% maximum
    Maximum Individual Metal Impurity 5 ppm
    Total Metal Impurities Below 50 ppm
    Storage Condition Keep in a tightly closed container, protected from light, moisture, and heat
    Shelf Life 12 months from date of manufacture under recommended storage

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

    Packing & Storage
    Packing Sealed glass bottle with tamper-evident closure, labeled for safety. Contains 100 grams of BASF Electronic Grade Gold Salt for electroplating.
    Container Loading (20′ FCL) 20′ FCL: packaged gold plating salt on pallets, secured with dunnage, labeled for electronic-grade chemical transport. Ensure hazard compliance.
    Shipping This material is classified as hazardous and requires compliant packaging, labeling, and documentation for transport. Ship via ground freight or air cargo, adhering to IATA, IMO, and DOT regulations. Use authorized containers, protect from moisture, and ensure proper segregation. Handling by trained personnel is mandatory.
    Storage Store in a tightly sealed, clearly labeled original container in a cool, dry, well-ventilated area. Keep away from acids, oxidizing agents, heat sources, and direct sunlight. Maintain strict cleanliness to prevent contamination, as electronic/EL grade purity is critical. Use dedicated equipment, avoid moisture, and follow all hazardous material handling protocols.
    Shelf Life Shelf life is typically 24 months from manufacture date if stored sealed in a cool, dry area away from light.
    Application of Gold Plating Salt (BASF Electronic Grade Gold Salt) Electronic/EL Grade

    Semiconductor Wafer Bumping: Sulfite Gold Chemistry Under Controlled Mass Transport

    Gold plating salt of electronic/EL grade from BASF is deployed in through-mask electroplating of gold bumps on 200 mm and 300 mm wafers for subsequent thermosonic flip-chip attach. The bath is prepared with gold metal concentration maintained between 8 g/L and 12 g/L, with the sulfite-based electrolyte adjusted to pH 6.8–7.2 at an operating temperature of 55 °C ± 2 °C. Anode material is typically platinized titanium mesh, dimensionally stable under the applied cell potential. The deposition cell is a fountain-type plater, examples including Semitool Raider ECD and ACM Research Ultra ECP platforms, with wafer rotation speed set at 20–60 rpm and electrolyte flow rate between 10 L/min and 25 L/min across a 300 mm wafer surface. Current density is maintained at 0.2–0.6 A/dm² in direct-current mode with pulse interruption at 10 ms on / 90 ms off to suppress edge build-up. Under these parameters, plating rate ranges from 0.15 µm/min to 0.35 µm/min, yielding bump height uniformity within-wafer of ≤ 5 % (σ/mean) as verified by four-point probe sheet resistance mapping and stylus profilometry across 49 fixed measurement sites. Mask adhesion failure is documented on production lines when bath temperature exceeds 62 °C, causing photoresist lifting at the bump base due to thermal stress differential between the patterned dry film and the electrodeposited gold. Gold bump purity after deposition is ≥ 99.99 wt % by glow discharge mass spectrometry, meeting the impurity ceiling for alkali metals (Na ≤ 5 ppm, K ≤ 10 ppm) specified in SEMI S8 and SEMI F47 factory interface standards. After plating, the wafer is subjected to a 30-minute deionized water cascade rinse at resistivity ≥ 18 MΩ·cm to eliminate residual sulfite, which otherwise causes pitting corrosion at the gold-nickel interface during subsequent reflow at 280 °C for 5 min. A two-stage anneal at 150 °C for 60 min in nitrogen atmosphere bleeds co-deposited hydrogen, reducing film stress from approximately 150 MPa to 60 MPa as measured by wafer bow curvature change. The terminal gold bump is compatible with Au stud bump bonding onto Al pad metallization, with shear force per bump exceeding 12 gf for a 60 µm × 60 µm bump area according to JESD22-B117A testing.
    ParameterRangeEffect on Deposit
    Gold ion concentration8–12 g/LAbove 12 g/L: roughness increases; below 8 g/L: mass transport limitation
    Operating temperature53–57 °CAbove 57 °C: sulfite decomposition accelerates; below 53 °C: current efficiency drops below 85 %
    Current density0.2–0.6 A/dm²Above 0.6 A/dm²: nodule formation and photoresist lifting
    pH6.8–7.2Outside range: excessive hydrogen evolution or gold salt precipitation
    The bath is replenished with gold salt addition calculated from ampere-hour meters on the rectifier, with replenishment interval set at every 4 hours of continuous plating. Bath aging is monitored by cyclic voltammetric stripping at 10 mV/s in a three-electrode cell with saturated calomel reference, and the bath is discarded when sulfite oxidation product exceeds 5 g/L as sulfate. Published data for extended bath life beyond 8 metal turnovers is limited for this specific electronic-grade formulation.

    What Limits Cyanide-Based Gold Deposition on PCB Finger Contacts?

    Edge connector fingers on high-reliability printed circuit boards are plated with gold from potassium gold cyanide derived from the electronic/EL grade salt, dissolved to a gold metal content of 4–8 g/L in a citric acid–potassium citrate buffer at pH 9.0 ± 0.3. The bath operates in an insoluble anode cell using 316L stainless steel anodes at 58–65 °C, with air agitation at 1.5–3.0 L/min per 100 L of bath volume plus cathode rod reciprocation at 1.5–2.5 m/min. Current density is confined to 0.1–0.3 A/dm² in direct-current mode because higher densities cause cyanide decomposition at the anode and organic brightener combustion at the cathode, manifesting as brownish deposit streaks along the finger edges. Nickel underlayer is plated first to a thickness of 2.5–5.0 µm per ASTM B488 Table 1 and AMS-QQ-N-290B, with gold thickness specified at 0.75–1.5 µm for commercial USB and PCIe connector fingers and 2.5 µm minimum for military applications under MIL-DTL-45204 Type II Grade C. The cyanide formulation incorporates a cobalt brightener at 50–150 mg/L as Co, which co-deposits at 0.1–0.3 wt % in the gold film and is responsible for hardness values of 130–200 HV₀.₀₂₅ per Vickers microindentation. Porosity of the gold deposit, measured by ASTM B735 nitric acid vapor porosity test or electrographic ENIG testing, is specified at ≤ 1 pore/cm² after 60-second exposure. Higher cobalt content increases deposit hardness but reduces ductility; wire bonding and soldering applications on the same finger require an upper cobalt ceiling of 0.3 wt %, above which gold-tin intermetallic formation is retarded. A cyanide degradation byproduct, potassium carbonate, accumulates at 5–15 g/L per 1000 Ah of bath operation; carbonate levels above 75 g/L narrow the plating window and mandate partial bath discard. Replacement of the gold salt is performed using the electronic/EL grade material exclusively, because technical-grade gold cyanide introduces copper, iron, and lead impurities at levels that measurably shift deposit color and porosity.

    When Sulfite Gold Chemistry Replaces Cyanide in MEMS Fabrication

    Microelectromechanical systems with photoresist-defined seed metallization require gold electroplating through thick resist molds, typically SU-8 or AZ 9260 negative-tone resists, which are attacked by alkaline cyanide baths. The sulfite-based gold salt of electronic/EL grade is dissolved to a metal concentration of 10–16 g/L with sulfite ion held at 40–60 g/L as SO₃²⁻ and sulfate as an inert electrolyte. Plating temperature is limited to 40–45 °C because the UV-exposed SU-8 structure begins thermal flow above 55 °C, and because gold sulfite electrolyte decomposes autocatalytically above 50 °C, producing metallic gold precipitate in the bath volume. Current density in DC mode is set at 0.15–0.25 A/dm² in a paddle cell with paddle speed 15–30 cm/s and gap distance 2.5 cm between anode and cathode. Deposit stress is managed by thallium addition as a grain refiner at 5–15 mg/L; without thallium, tensile stress exceeds 180 MPa and causes cantilever bending in released MEMS structures. Gold film thickness for RF MEMS switching devices ranges from 2.0 µm to 6.0 µm, requiring continuous plating times of 10–30 minutes at the specified current density. After electroplating, the photoresist mold is stripped in NMP at 80 °C for 30 min followed by O₂ plasma descum at 300 W, 100 mTorr, 10 min; residual sulfite in the deposit caused by insufficient rinsing is quantified by X-ray photoelectron spectroscopy sulfur 2p peak at binding energy 162 eV, and failure to maintain sulfur below 0.5 at % results in contact resistance drift on MEMS switch terminals exceeding 20 % over 10⁷ cycles measured under ASTM B845-97. A sacrificial silicon dioxide layer beneath the gold is etched in buffered hydrofluoric acid after plating; the gold film must demonstrate etch resistance with weight loss below 0.1 % after 60-second immersion, a requirement that mandates high-purity electronic grade salt rather than technical grade material containing transition metal catalysts.Thermal budget constraints in optoelectronic packaging require gold deposition on III-V compound semiconductor substrates without exceeding the wafer processing temperature ceiling of 110 °C for InP-based lasers and 150 °C for GaAs-based devices. The electronic/EL grade gold salt is formulated as a cyanide-free sulfite bath operating at 35–42 °C because lower plating temperature reduces thermal diffusion of gold into the semiconductor and preserves the integrity of pre-deposited Au/Zn/Au p-contact layers. Gold thickness on the p-side bonding pad is specified at 1.0–2.0 µm to enable AuSn eutectic die attach at 280–300 °C; the deposit must be free of cyanide-derived carbon contamination because interstitial carbon above 200 ppm measured by secondary ion mass spectrometry degrades AuSn wetting, increasing void density in the solder joint to above 5 % by scanning acoustic microscopy. The sulfite gold deposit on n-side contacts serves as a wire bonding surface for 25 µm diameter gold wire; ball shear test force per JESD22-B116B must exceed 8 gf and cratering of the underlying GaAs must be absent at 500× magnification. A barrier layer of platinum or palladium, typically 0.1–0.3 µm thick, is sputtered between the gold plating and the semiconductor to prevent gallium out-diffusion during subsequent high-temperature assembly steps. The plating bath is filtered through 0.2 µm polypropylene cartridge filters, and the filter must be replaced after every 500 L of throughput to maintain particle counts below 10 particles/mL in the 0.5 µm size range per SEMI C79 particle measurement guideline.

    Medical Microelectrode Plating and FDA 21 CFR Compliance

    Implantable neural recording electrodes and pacemaker connector surfaces are electroplated with gold from BASF electronic/EL grade gold salt that is processed under ISO 13485 quality management and supplied with certificates of analysis covering residual metal impurities to ≤ 10 ppm total. Bath formulation for medical microelectrode plating uses gold concentration of 8–12 g/L in a citric acid buffer at pH 6.5–7.0, with operating temperature held at 50–55 °C and current density restricted to 0.1–0.2 A/dm². The reduced current density minimizes grain size to below 100 nm as determined by X-ray diffraction line broadening using the Scherrer equation on the gold (111) reflection at 2θ = 38.2°. Electrode impedance at 1 kHz in physiological saline is required to be below 200 kΩ for a 50 µm diameter microelectrode site per ASTM F2129 electrochemical testing; smoother gold films from low-current plating show impedance values 10–30 % lower than rough deposits from higher current densities. Biocompatibility assessment follows ISO 10993-5 for cytotoxicity with L929 fibroblast cells, requiring cell viability ≥ 70 % after 24-hour elution exposure. The finished gold-plated device is subjected to cleaning in isopropanol at 40 kHz ultrasonic frequency for 10 min followed by USP-grade water rinse, because residual cyanide or sulfite ions from the plating salt on implant surfaces are limited to ≤ 1 µg/cm² by ion chromatography of the extraction fluid. The material safety documentation for BASF electronic grade gold salt contains the REACH registration dossier, and the downstream medical plating facility must maintain a Device Master Record under FDA 21 CFR Part 820 specifying the plating bath composition, the salt lot number, and the plating parameters for each batch of finished devices.Aerospace-grade separable connector contacts are plated from the same electronic/EL grade gold salt in either cyanide-based hard gold chemistry or sulfite-based soft gold chemistry depending on contact mating cycles. Hard gold for connector pins and sockets is deposited from a cobalt-alloyed cyanide bath at 60–65 °C and 0.2–0.4 A/dm² to a thickness of 1.25–2.5 µm, meeting MIL-DTL-45204 Type II Grade C hardness requirements of 130–200 HK₂₅ (Knoop). Underplate nickel is plated to 3.75–5.0 µm per AMS-QQ-N-290B Grade L, and the combined coating must withstand 100 cycles of mating and unmating with contact resistance increase below 5 mΩ measured per EIA-364-23. Barrel plating of small connector contacts utilizes rotational speed of 8–12 rpm with dangler current distribution; excessive barrel loading above 60 % fill results in non-uniform gold thickness below the specification limit, a failure documented on production lines when the load exceeds 500 g per 10 L barrel. Salt spray exposure per ASTM B117 for 96 hours on finished connectors requires no visible corrosion products on the gold surface and no base metal exposure through pores, a criterion that forces the porosity specification to ≤ 2 pores/cm² at 1.25 µm gold thickness. The gold plating solution is analyzed by atomic absorption spectroscopy every 8 operating hours, and the gold metal concentration is maintained within ± 0.5 g/L of the nominal set point by addition of the electronic/EL grade salt, because concentration drift beyond that band shifts the deposit alloy composition and hardness outside the MIL specification envelope.The electronic/EL grade gold salt is also applied in electroforming of X-ray collimator apertures and micro-nozzle components where dimensional tolerance demands are tighter than standard plating operations. Electroforming baths are configured with gold concentration at 12–20 g/L in a sulfite electrolyte, operated at 45–50 °C and 0.3–0.8 A/dm², with mandrel rotation at 60 rpm to ensure thickness uniformity across the mandrel surface. Deposit thickness for collimator aperture walls is specified at 25–75 µm, requiring continuous plating times of 4–12 hours; dimensional deviation across the aperture array is held to ± 2 µm by periodic reversal at 5 % duty cycle to suppress nodular growth. The mandrel is fabricated from machined aluminum with a sacrificial copper strike thickness of 0.5 µm; after gold electroforming, the aluminum is dissolved in sodium hydroxide at 60 °C without attacking the gold shell. Internal stress of the electroformed gold, measured by rigid strip method per ASTM E837, must remain below 50 MPa compressive to prevent aperture wall distortion upon mandrel removal. The electronic/EL grade salt is specified because chloride contamination in technical grade gold salts above 20 ppm causes pitting corrosion in the electroformed walls during subsequent acid cleaning, and pit density measured by scanning electron microscopy exceeds 3 pits/mm², rendering the part non-conforming for collimator optical performance.High-frequency RF shielding on ceramic substrates is fabricated by screen printing or photolithographic patterning of gold conductive traces, followed by electroless or electrolytic gold thickening from the electronic/EL grade salt. Electrolytic thickening is performed in a rack fixture with current density of 0.1–0.3 A/dm² at 50–55 °C in a sulfite bath to avoid attack of screen-printed dielectric glass that is soluble in cyanide solutions above pH 9.5. Gold thickness on shield walls is specified at 3–5 µm to achieve RF shielding effectiveness of ≥ 60 dB across the frequency range 1–18 GHz when measured by IEEE 299 shielded enclosure method. Trace resistivity after plating is measured at ≤ 3.0 µΩ·cm, and surface roughness Ra below 0.8 µm is required to minimize conductor loss at millimeter-wave frequencies. The gold salt batch must exhibit absence of silver contamination, because even 50 ppm silver co-deposition increases conductor resistivity and causes intermodulation distortion in RF shield applications, a failure mode confirmed by two-tone third-order intermodulation testing per IEC 62037. The plating operation is conducted inside a cleanroom rated ISO Class 8, and the bath is blanketed with nitrogen to prevent sulfite oxidation that would otherwise generate thiosulfate byproducts which brighten the deposit but co-deposit sulfur at levels above 0.3 at %, raising RF loss tangent.
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    Certification & Compliance
    More Introduction

    The BASF Electronic Grade Gold Salt, supplied under the Electronic/EL Grade designation, is a cyanide-based potassium dicyanoaurate(I) raw material for make-up and replenishment of electroplating baths used in semiconductor packaging, connector fabrication, leadframe plating, and printed circuit board final finishing. The product carries CAS number 13967-50-5, empirical formula KAu(CN)2, and molecular weight 288.10 g/mol. Theoretical stoichiometric gold content is 68.37% w/w; the commercial electronic grade is commonly specified at 68.2% w/w nominal gold with lot-specific assay verification. The material is supplied as a white crystalline solid, not as a ready-to-use plating solution, and must be dissolved in an alkaline cyanide matrix before use. It is not a brightener, grain refiner, or hardness modifier; cobalt, nickel, and organic additive packages are introduced as separate components.

    The Electronic/EL designation is a release grade rather than a distinct chemical species. It identifies a potassium dicyanoaurate(I) material controlled for trace metallic impurities that affect deposit appearance, solderability, and long-term bath stability. The product may be ordered under regional material codes, but the certificate of analysis is the binding quality document. For the same reason, the product cannot be treated as a direct drop-in for every proprietary gold electrolyte; the exact make-up, replenishment rate, and additive balance remain specific to the plating bath being used.

    What Distinguishes the Electronic/EL Grade from Technical-Grade Potassium Gold Cyanide?

    The principal difference is the analytical release panel rather than the gold stoichiometry. Technical-grade potassium gold cyanide is commonly sold on gold assay and appearance, whereas the Electronic/EL material is released with a lot-specific certificate that includes trace-metal quantification by ICP-OES after cyanide matrix digestion. The reported elements typically include Na, Fe, Cu, Ni, Pb, Cd, Zn, Ag, Pt, and Pd; some purchase specifications add Cr and Mn. Exact element-specific limits are customer-defined and confirmed against certified reference materials; across electronic-grade potassium gold cyanide, the most frequently constrained elements are Fe, Cu, Ni, Pb, and Cd. Published data for a single universal impurity threshold applicable to all proprietary baths is limited.

    Gold deposits from cyanide electrolytes are evaluated for solder wetting using a wetting balance in accordance with IEC 60068-2-54 or IPC-J-STD-003C. The salt itself is not the direct test subject, but uncontrolled metallic contamination in the replenisher can shift wetting time and wetting force after thermal aging. In high-speed lines, the lower trace-metal variability is intended to reduce the frequency of deposit roughness, nodulation, and solderability excursions. Technical-grade material may contain sufficient chloride or trace metal variability to require increased dummy plating and more frequent carbon treatment; the Electronic/EL grade is expected to be used where bath maintenance intervals are fixed and process windows are narrow.

    Dissolution of the Electronic/EL Grade is performed in deionized water with resistivity at or above 18 MΩ·cm at 40–50 °C. The dissolution tank is typically polypropylene or PVDF; stainless steel is not recommended for free-cyanide service because of stress-corrosion cracking and passive-film instability in alkaline cyanide environments. The salt is added under mechanical agitation to an aqueous solution already containing the required free potassium cyanide. Adding the solid to acid or to an acidic plating bath is prohibited because cyanide salts liberate hydrogen cyanide at low pH; cyanide gold baths are normally maintained at pH 9.0–10.5. In a conventional bath, the gold metal concentration is commonly 8–20 g/L with free potassium cyanide at 15–30 g/L, but the exact ratio is dictated by the proprietary wetting agent and grain-refining system. Transfer from the makeup tank to the production sump is by double-diaphragm pump or vacuum transfer; air agitation is not used during dissolution because it accelerates carbonate formation and can cause localized oxidation of free cyanide.

    When the Salt Is Charged into High-Speed Reel-to-Reel Selective Plating Lines

    In reel-to-reel connector and leadframe plating, the dissolved potassium dicyanoaurate is used to maintain gold metal concentration in cobalt- or nickel-hardened gold electrolytes. Deposition is carried out in jet-plating cells or brush-plating cells with insoluble platinized titanium anodes. Typical operation uses current densities between 5 A/dm² and 20 A/dm², electrolyte temperature between 50 °C and 65 °C, and line speed up to 5 m/min for thin selective deposits; the exact window is set by the additive supplier, cell manifold design, and anode-to-cathode spacing. Rectifier ripple should be below 5% RMS because elevated ripple increases deposit stress and reduces brightness in cobalt-hardened gold.

    The Electronic/EL Grade is preferred where the electrolyte is filtered continuously through 0.2–0.5 µm polypropylene depth filters. Low-level insoluble matter and trace-metal variability in technical salt can increase filter loading and cause localized flow restriction at the cell inlet. In selective plating, the local current density at the leading edge of the deposited stripe may be several times the average cell current density; therefore any metallic contamination that shifts the onset of burning or nodulation has an outsized effect on yield. Bath performance is confirmed by Hull cell panels and by cross-section thickness measurement according to ASTM B487. The salt does not supply cobalt or nickel to the deposit; hardness is developed from separate proprietary concentrates or inorganic salts and is measured with a Knoop microindenter in accordance with ASTM B578.

    Within electronics manufacturing, the Electronic/EL Grade is used primarily in cyanide hard gold formulations for separable connectors, edge-card contacts, and leadframes. These deposits are commonly cobalt-hardened with gold purity of 99.0–99.7% by weight in the solid metal and hardness from 130 HK to 200 HK on a Knoop indenter. The product is not intended for electroplating of pure soft gold bumps from cyanide-free sulfite systems, where the gold source is normally sodium gold sulfite rather than potassium dicyanoaurate. The choice between cyanide and sulfite gold is dictated by photoresist compatibility and deposit stress: sulfite-based soft gold is preferred for wafer bumping under thick positive photoresist, while cyanide hard gold is used where wear resistance and low contact force are required. Published data for direct substitution of this salt into sulfite baths is limited; substitution is not recommended without reformulation.

    Deposit Qualification Standards and Test Coupons

    Gold deposits produced from baths replenished with this salt are qualified against electronics coating specifications rather than against the salt alone. Commonly referenced deposit specifications include MIL-DTL-45204D for electrodeposited gold coatings, ASTM B488-18 for engineering gold deposits, and ISO 27874:2008 for electrodeposited gold and gold alloy coatings for engineering applications. Thickness verification is performed by X-ray fluorescence, coulometric methods, or cross-sectional microscopy; adhesion is assessed by tape or bend methods from ASTM B571, porosity by nitric acid vapor exposure under ASTM B735, and hardness by ASTM B578. The table below summarizes the test methods frequently referenced for qualification of connector, leadframe, and pad finishes.

    Common qualification methods for electronic gold deposits
    PropertyReference methodTypical equipment
    ThicknessASTM B568 / ASTM B487 / ISO 2177X-ray fluorescence unit, optical microscope, coulometric tester
    HardnessASTM B578Knoop microindenter
    AdhesionASTM B571Tape/peel and bend fixtures
    PorosityASTM B735Nitric acid vapor chamber
    SolderabilityIPC-J-STD-003C / IEC 60068-2-54Wetting balance

    Lot release for the salt itself includes a certificate of analysis that may report gold assay, trace metal impurities, chloride and sulfate, and appearance. Gold assay is commonly determined by gravimetric fire assay or an equivalent high-precision method. Trace metal testing by ICP-OES requires alkaline cyanide digestion followed by cyanide destruction before introduction to the instrument; this is an internal method audited under ISO/IEC 17025. Ion chromatography may be used for chloride and sulfate screening. The specific reporting limits are set by the purchase specification rather than by a generic grade definition.

    Because the material is a process chemical rather than a finished article, REACH registration and CLP notification apply within the European Economic Area. RoHS is not directly applicable to the salt, but the resulting deposit must meet applicable substance restrictions when placed onto finished electrical and electronic equipment. The deposited gold alloy may contain cobalt or nickel; those elements are added separately as proprietary hardeners or inorganic salts and are not supplied by this salt.

    Purity Controls Are Not a Substitute for Bath Purification

    Even with the Electronic/EL Grade, production baths accumulate contamination from drag-in of copper and nickel process solutions, substrate residues, airborne particulates, and organic additive decomposition. Metallic impurities must be monitored by ICP-OES on a scheduled frequency; the schedule is determined by the product mix, with dummy plating at low current density used to remove co-depositable metals such as Cu and Ni. The salt addition does not remove carbonates, which accumulate in cyanide baths from alkaline hydrolysis and atmospheric carbon dioxide absorption; elevated carbonate can narrow the bright range and reduce cathode efficiency. Activated carbon treatment at 2–5 g/L may be used to reduce organic breakdown products, but it also removes wetting agents and grain refiners and must be followed by additive adjustment and Hull cell verification.

    The product must not be combined with ammonium salts because ammonia can complex gold and alter deposition. Contact with mineral acids, acid salts, and strong oxidizers is prohibited; cyanide baths must be segregated from acidic process chemistries. Fume hoods serving cyanide and acid operations should not share exhaust ducts unless the scrubber is specifically designed for hydrogen cyanide. Storage containers should be sealed and constructed of linear low-density polyethylene, high-density polyethylene, or PVDF; unlined steel and aluminum are not suitable for cyanide contact. Spill and rinse streams must be collected and treated by alkaline chlorination or an approved equivalent before discharge, with residual total cyanide measured by an ion-selective electrode or colorimetric autoanalyzer in accordance with the site discharge permit.

    The cyanide complex is stable in alkaline solution but releases hydrogen cyanide as the pH is depressed. The bath pH must never be adjusted downward with acid unless a scrubber and continuous HCN monitoring are in place. In production-scale lines, the Electronic/EL Grade is therefore a controlled input, not a purification device; its benefit is realized only when the bath maintenance protocol is held constant and all additions are recorded on a per-ampere-hour basis.

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