| 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 | 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. |
| Parameter | Range | Effect on Deposit |
|---|---|---|
| Gold ion concentration | 8–12 g/L | Above 12 g/L: roughness increases; below 8 g/L: mass transport limitation |
| Operating temperature | 53–57 °C | Above 57 °C: sulfite decomposition accelerates; below 53 °C: current efficiency drops below 85 % |
| Current density | 0.2–0.6 A/dm² | Above 0.6 A/dm²: nodule formation and photoresist lifting |
| pH | 6.8–7.2 | Outside range: excessive hydrogen evolution or gold salt precipitation |
Competitive Gold Plating Salt (BASF Electronic Grade Gold Salt) Electronic/EL Grade prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
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.
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.
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.
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.
| Property | Reference method | Typical equipment |
|---|---|---|
| Thickness | ASTM B568 / ASTM B487 / ISO 2177 | X-ray fluorescence unit, optical microscope, coulometric tester |
| Hardness | ASTM B578 | Knoop microindenter |
| Adhesion | ASTM B571 | Tape/peel and bend fixtures |
| Porosity | ASTM B735 | Nitric acid vapor chamber |
| Solderability | IPC-J-STD-003C / IEC 60068-2-54 | Wetting 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.
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.