| HS Code | 260549 |
| Product Name | PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) |
| Grade | Electronic/EL Grade |
| Appearance | Clear liquid |
| Color | Blue to dark blue solution |
| Odor | Slight acidic odor |
| Ph | Strongly acidic, pH < 1 |
| Specific Gravity 20c | Approximately 1.05 to 1.25 g/cm3 |
| Copper Ion Concentration | Typical 2 to 5 g/L |
| Sulfuric Acid Concentration | Typical 50 to 100 g/L |
| Chloride Ion Concentration | Typical 20 to 60 mg/L |
| Purity Level | Electronic/EL grade with controlled low metal impurities |
| Filtration Rating | Filtered to ≤ 0.5 micrometer |
| Viscosity 20c | Near water-like viscosity |
| Boiling Point | Approximately 100°C as aqueous solution |
| Flash Point | Non-flammable, aqueous based |
| Storage Temperature | 5 to 35°C |
| Shelf Life | Typically 6 months in sealed original container |
| Solubility In Water | Fully miscible with water |
As an accredited PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25L HDPE drums, this electronic/EL grade solution ensures high-purity PCB hole metallization for horizontal copper plating. |
| Container Loading (20′ FCL) | 20′ FCL loaded with sealed HDPE drums on pallets, safely secured and labeled for Guanghua horizontal copper plating solution, electronic/EL grade. |
| Shipping | Ship as hazardous chemical, UN 3264 (corrosive liquid), PG II/III. Use leak-proof HDPE containers, upright, in ventilated, dry containers. Avoid heat, moisture, and incompatible materials. Comply with IATA/IMDG/ADR. Label as "Corrosive." Store at 15–25°C, away from acids/alkalis, and document EL grade purity declaration. |
| Storage | Store in a tightly sealed original container in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Keep separate from acids, oxidizers, and incompatible chemicals. Maintain recommended temperature range, avoid freezing, and ensure secondary containment to prevent leakage. Use proper labeling and handling procedures. |
| Shelf Life | Shelf life is typically 6 months from manufacture when stored sealed, at room temperature, away from sunlight and contamination. |
| Scenario | Governing Standard | Inspection Point | Acceptance Metric |
|---|---|---|---|
| Multilayer PCB through-hole metallization | IPC-6012E Class 3 | Through-hole wall copper after electrolytic plating | 20–25 μm minimum, thermal stress 288 °C 10 s |
| HDI microvia seed layer | IPC-6016C | Microvia wall copper and fill dimple | 6–10 μm wall, ≤ 5 μm dimple |
| Flexible and rigid-flex circuits | IPC-6013E Class 3 | Copper peel strength on polyimide | 0.8–1.2 N/mm, dimensional stability ±0.10% |
| IC substrate mSAP/SAP | IPC-6012E, JIS C 5012 | Seed layer roughness and alkali metal contamination | Ra ≤ 0.03 μm, <0.5 μg/cm² |
| Automotive powertrain and ADAS | IATF 16949, IPC-6012E Class 3 | Thermal shock resistance | 1,500 cycles -40 °C to 125 °C, R change <10% |
| High-frequency and mmWave boards | IPC-4101D, IPC-6018 | Hole wall pull-away after reflow | 6× 260 °C reflow, resin recession ≤ 5 μm |
| Segment | Concentrate Ratio | pH | HCHO | Seed Cu Thickness | Dwell Time |
|---|---|---|---|---|---|
| Multilayer rigid PCB | 18–22 vol% | 12.5–12.8 | 4.5–5.5 mL/L | 0.35–0.65 μm | 6–9 min |
| HDI microvia | 12–15 vol% | 12.3–12.5 | 3.0–4.0 mL/L | 0.25–0.45 μm | 5–7 min |
| Flex and rigid-flex | 15–18 vol% | 12.3–12.5 | 3.5–4.5 mL/L | 0.25–0.50 μm | 5–8 min |
| IC substrate | 16–20 vol% | 12.3–12.6 | 3.0–3.5 mL/L | 0.30–0.45 μm | 4–6 min |
| Automotive rigid PCB | 20–25 vol% | 12.5–12.8 | 4.5–6.0 mL/L | 0.45–0.80 μm | 10–14 min |
| High-frequency laminate | 14–18 vol% | 12.3–12.6 | 3.0–4.0 mL/L | 0.25–0.40 μm | 6–10 min |
Competitive PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) 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 product designated as the Guanghua Technology Horizontal Copper Plating Solution, Electronic/EL grade, is a multi-component acid copper electrolyte for direct-current or pulse horizontal conveyorized through-hole metallization in printed circuit board fabrication. The supplier model identifier commonly recorded in batch documentation is GH-HC-EL, with separate component codes for the copper sulfate/sulfuric acid make-up concentrate, brightener, carrier/suppressor, leveler, and replenisher. The operating bath is prepared from copper sulfate pentahydrate and sulfuric acid; typical diluted-bath concentrations are 55–75 g/L copper ion and 180–230 g/L sulfuric acid. Chloride concentration is maintained at 40–70 mg/L. Organic additive concentrations are not expressed as absolute gravimetric values in production baths because the brightener, carrier, and leveler are proprietary; their balance is monitored by cyclic voltammetric stripping and ampere-hour replenishment. The electronic/EL grade designation indicates a low trace metal tolerance grade, with electronic-grade lot release commonly targeting total trace metal impurities below 1 mg/L in the diluted bath, although published certificate-of-analysis limits for this specific formulation are limited. The make-up and replenisher components are supplied in 200 L HDPE drums, while organic additive packages are supplied in 20 L or 25 L closed drums classified as corrosive and requiring secondary containment.
This chemistry is intended as the electrolytic thickener after electroless copper seed or direct metallization, not as a primary conductive seed. It is applied on horizontal lines to metallize through-holes, blind vias, and microvias in HDI, rigid-flex, and multilayer boards where the final copper layer is specified to 20–35 µm according to IPC-6012 class requirements. At a cathodic current density of 3.0 A/dm², acid copper deposition rate in high-throw horizontal configurations is approximately 0.8–1.2 µm/min; published data for this specific GH-HC-EL formulation is limited. The solution is compatible with insoluble iridium-tantalum-coated titanium anodes used in horizontal cells and requires continuous electrolyte filtration through 10 µm polypropylene or acrylic cartridges. Deionized water used for make-up should have resistivity of at least 5 MΩ·cm to avoid alkaline-earth precipitation and sulfate scale formation.
In vertical acid copper tanks, solution exchange inside a high-aspect-ratio through-hole is dominated by natural convection and bath agitation. In horizontal cells, electrolyte is flooded or sprayed through the hole at nozzle flow rates of 3–6 L/min, creating forced convection perpendicular to the board surface. This impingement raises the limiting current density at the hole center and shifts copper distribution from the dog-bone profile typical of diffusion-limited vertical plating. Haring-Blum throwing power measurements for high-acid horizontal formulations generally fall between 60–85% at 2.0 A/dm²; published data for this specific GH-HC-EL system is limited. On production equipment with working width 1300 mm and conveyor speed 1.0–1.5 m/min, thickness variation between board surface and hole center has been observed below 10% for aspect ratio 8:1 when current density is held at 2.5–3.5 A/dm². The critical process variable is not only current density but also nozzle-to-board alignment; clogged nozzles create local starvation and should be checked against flow-meter readings rather than visual output.
Horizontal plating cells used with this chemistry are typically arranged as flooded sections with submerged nozzles above and below the panel. The anode-cathode gap is maintained at 15–30 mm, and overall rectifier voltage runs between 2.5 V and 5.0 V depending on bath conductivity and board loading. Bath temperature is controlled at 22–28 °C; excursions above 30 °C accelerate organic additive oxidation and may increase surface roughness at high current density. Filtration and carbon treatment of a side stream at 0.5–1.0% of bath volume per hour are used to remove organic breakdown products. Air entrainment at the sump is a known production bottleneck; pump cavitation from entrained air produces flow instability and local copper thickness loss. Sump level control within ±5 mm and de-aeration screens are therefore critical. Unopened components have a nominal shelf life of 12 months at 5–35 °C; after make-up, bath life is determined by chloride and additive balance, not by a fixed calendar interval.
The operable window for chloride is narrow. Below 40 mg/L, the adsorptive leveling complex is insufficient, and deposits tend toward dull, rough surfaces at current densities above 2.5 A/dm². Above 80 mg/L, chloride can attack insoluble anode coatings and precipitate copper(I) chloride, increasing nozzle blockage and reducing anode life. Copper concentration below 55 g/L reduces conductivity and requires higher rectifier voltage; above 75 g/L, sulfate solubility constraints become more sensitive to temperature cycles. Sulfuric acid below 180 g/L lowers electrolyte conductivity and may reduce throwing power. Above 230 g/L, sulfate salt precipitation in pumps and sumps is observed during shutdowns below 15 °C. Organic additive balance is the dominant factor for deposit stress. Excess brightener reduces surface roughness but increases tensile stress; excess leveler refines grain size but can push internal tensile stress above 15 MPa and cause corner cracking after thermal stress testing under IPC-TM-650 2.6.8. Consequently, ampere-hour dosing is preferred over visual control, and the supplier analytical parameters are set by cyclic voltammetric stripping rather than absolute concentration.
| Parameter | Operating window or control limit | Typical analytical or process control method |
|---|---|---|
| Copper ion | 55–75 g/L | ICP-OES |
| Sulfuric acid | 180–230 g/L | Acid-base titration |
| Chloride | 40–70 mg/L | Potentiometric titration |
| Bath temperature | 22–28 °C | PT100, sump or cell return |
| Cathodic current density | 2.0–3.5 A/dm² | Rectifier monitor |
| Deposition time for 20 µm | 10–20 min | Process control, current-density dependent |
| Anode type | Ir-Ta-coated titanium, insoluble | Supplier specification |
| Filtration | 10 µm cartridges | Polypropylene or acrylic |
Unlike conventional vertical acid copper processes that use soluble phosphorus copper anodes and often operate at 80–110 g/L copper, this horizontal formulation is configured for insoluble anode operation. The lower copper concentration and forced electrolyte flow are matched to the higher mass transport of horizontal cells. Compared with electroless copper seed baths, which deposit 0.5–1.0 µm of copper by chemical reduction, this product is an electrolytic thickener and produces the main plated-through-hole copper mass. It is not a replacement for direct metallization systems based on carbon, graphite, or conductive polymer, nor does it remove the need for desmear. The ordering is therefore desmear, electroless copper or direct metallization, and then horizontal electrolytic copper thickening. Against competing horizontal acid copper products, the Electronic/EL grade is differentiated by the low-chloride sensitivity of the additive package and by the reduction in deposit stress after thermal cycling; target tensile stress in the plated layer is below 10 MPa as evaluated by bent-cathode or foil methods, though public comparative data on this specific grade is limited. The electroplated copper also has electrical resistivity in the range 1.7–2.0 µΩ·cm, lower than the typical electroless copper seed range of 3–6 µΩ·cm. The chemistry avoids formaldehyde, which is used in some electroless copper process variants.
Above aspect ratio 10:1, forced impingement loses effectiveness because the hole center is still transport-limited relative to the board surface. If nozzle flow falls below 3 L/min, center wall thickness can fall below 15 µm while surface thickness reaches 25 µm, producing a dog-bone ratio above 1.6:1. Under IPC-TM-650 2.6.8 thermal stress testing at 288 °C for 10 s, thin center walls can fail by corner or barrel cracks after solder float. Boards entering the plating cell with excessive surface water dilute the acid locally; pre-treatment roller pressure and air knife settings must maintain entry board surface moisture below a threshold set by the line control plan. The solution is not recommended for boards with exposed tin or tin-lead finishes because metal dissolution into the acid bath contaminates the electrolyte and changes additive response. Drag-in of ammonia-based cleaners or waste strippers should be avoided because copper-amine complexes can form and interfere with leveler adsorption. Bath contamination by zinc, nickel, or iron above low mg/L levels reduces covering power and can produce pitting at high current density; ion-exchange or dummy plating is used to restore lot-to-lot consistency.
| Requirement or characteristic | Standard or method | Acceptance criterion |
|---|---|---|
| Plated-through-hole copper average thickness | IPC-6012 Class 3 | ≥25 µm average, ≥20 µm minimum wall |
| Thermal stress integrity | IPC-TM-650 2.6.8 | No internal cracks or plating separation after 288 °C, 10 s |
| Coating thickness measurement | ASTM B568 | X-ray fluorescence, calibrated to copper |
| Restriction of hazardous substances | Directive 2011/65/EU Annex II | No Pb, Cd, Hg, Cr(VI), PBB, PBDE above limits |
| REACH information | Regulation (EC) No 1907/2006 Article 33 | SVHC disclosure as applicable |
| Quality management | ISO 9001:2015 | Lot traceability, certificate of analysis |