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PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) Electronic/EL Grade

    • Product Name: PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) 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 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 & Storage
    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.
    Application of PCB Hole Metallization Solution (Guanghua Technology Horizontal Copper Plating Solution) Electronic/EL Grade
    In high-layer-count multilayer PCB production, the shift from batch vertical electroless copper to horizontal conveyorized hole metallization reduces tank residence time variability for panels with drilled hole diameters from 0.20 mm to 0.35 mm and board thickness from 2.4 mm to 4.0 mm. The working bath is prepared from the Electronic/EL Grade horizontal copper plating solution at 18–22 vol% in deionized water, with 37% formaldehyde maintained at 4.5–5.5 mL/L, sodium hydroxide dosed to pH 12.5–12.8, and cupric ion concentration held at 2.5–3.2 g/L by replacement of 0.15–0.25 L concentrate per 100 m² processed panel surface. The process operates in a horizontal line equipped with flooding nozzles at 0.18–0.25 MPa, squeegee rollers between stages, and a final cascade rinse of deionized water monitored at ≥ 1.0 MΩ·cm; conveyor speed is set between 0.8 m/min and 1.4 m/min to yield a deposited electroless copper layer of 0.35–0.65 μm on the epoxy-glass hole wall before subsequent acid copper electroplating. Compliance for this board type is anchored to IPC-6012E Class 3 through-hole copper requirements, with thermal stress test at 288 °C for 10 s, while material compliance against RoHS Directive 2011/65/EU Annex II and REACH Regulation (EC) No 1907/2006 Article 33 is verified by the chemical supplier’s certificate of analysis. The downstream fabrication sequence includes mechanical drilling of 600–1,200 holes/panel, alkaline permanganate desmear at 70–75 °C for 8–12 min, glass etch, neutralization, pre-dip, palladium catalyst adsorption, and the horizontal electroless copper deposition described above; after drying at 85–95 °C, panels proceed to pattern plating of electrolytic copper to a final through-hole wall thickness of 20–25 μm for Class 3 designs. Terminal finished products are multilayer PCBs installed in industrial control backplanes, server motherboards, and power conversion modules, where the metallization layer must survive solder float cycles at 288 °C without hole wall pull-away, interconnect separation, or blistering of the copper-resin interface.

    What Limits the Uniformity of Laser-Drilled Microvia Seed Layers in HDI Stacked-Via Structures?

    HDI panels with laser-drilled microvias of 75–100 μm diameter in 50–75 μm thin dielectric layers present a severe inverse relationship between via aspect ratio and convective solution exchange inside the via interior. For this application, the horizontal copper plating solution is diluted to 12–15 vol% to reduce viscosity and suppress excessive copper deposition at the via rim, while the reducer concentration is held at 3.0–4.0 mL/L of 37% formaldehyde and the operating pH is controlled between 12.3–12.5. Sodium hydroxide dosage is maintained at 7.5–9.0 g/L, and replenishment is performed by automatic level control tied to panel count, at 0.08–0.12 L concentrate per 10 m² processed panel area, with continuous filtration through 1 μm polypropylene cartridge elements to reduce palladium fines and copper particulate carryover. Downstream production equipment includes a six-chamber horizontal electroless copper line with ultrasonic agitation at 40 kHz in the pre-wetting and activator chambers, flood bars at 0.20–0.25 MPa, and final rinse quality of 1.5 MΩ·cm minimum; the subsequent via fill is performed in a vertical continuous plating line with insoluble anodes and organic leveling additives to achieve 8–12 μm copper fill thickness within 40–60 min, with dimple depth after fill controlled to ≤ 5 μm for subsequent lamination. Governing standards for the HDI board include IPC-6016C for high-density interconnect qualification, with microvia copper wall thickness inspected at 6–10 μm and solder-shock adhesion tested per IPC-TM-650 method 2.4.13; compliance with RoHS Directive 2011/65/EU and REACH SVHC obligations is verified on the plating solution and its sub-components. Terminal finished products are smartphone mainboards, tablet system boards, wearable sensor modules, and camera module substrates, where the electroless seed layer must establish a void-free interface between the laser-drilled polymer surface and the electrolytic fill deposit.
    Compliance and Test Method Matrix for Horizontal Electroless Copper Application Segments
    ScenarioGoverning StandardInspection PointAcceptance Metric
    Multilayer PCB through-hole metallizationIPC-6012E Class 3Through-hole wall copper after electrolytic plating20–25 μm minimum, thermal stress 288 °C 10 s
    HDI microvia seed layerIPC-6016CMicrovia wall copper and fill dimple6–10 μm wall, ≤ 5 μm dimple
    Flexible and rigid-flex circuitsIPC-6013E Class 3Copper peel strength on polyimide0.8–1.2 N/mm, dimensional stability ±0.10%
    IC substrate mSAP/SAPIPC-6012E, JIS C 5012Seed layer roughness and alkali metal contaminationRa ≤ 0.03 μm, <0.5 μg/cm²
    Automotive powertrain and ADASIATF 16949, IPC-6012E Class 3Thermal shock resistance1,500 cycles -40 °C to 125 °C, R change <10%
    High-frequency and mmWave boardsIPC-4101D, IPC-6018Hole wall pull-away after reflow 260 °C reflow, resin recession ≤ 5 μm

    Polyimide Substrate Metallization and Dynamic Bend Fatigue

    Flexible and rigid-flex circuits built on 25 μm polyimide cores impose a metallization layer that must function both as a seed for electrolytic plating and as a flexural conductor in dynamic bending regions; the electroless copper deposit is therefore required to withstand cyclic strain without interfacial fracture. A reduced working concentration of 15–18 vol% is used for flex panels, with pH maintained at 12.3–12.5 and formaldehyde concentration set at 3.5–4.5 mL/L because excessive alkalinity can embrittle the polyimide surface and reduce direct copper-to-polyimide adhesion after the initial electroless strike. Stabilizer addition is kept at 0.8–1.2 mL/L for a bath age of 12–16 metal turnover cycles, beyond which the bath is discarded due to accumulation of dissolved organics from adhesive and coverlay materials. The horizontal line is configured with soft polypropylene rollers, low panel tension of 3–5 N/cm panel width, and dual-sided flooding at 0.12–0.18 MPa to minimize crease formation; after chemical copper deposition of 0.25–0.50 μm, panels are transfer-dried at 80 °C before electrolytic copper plating to a total conductor thickness of 18–25 μm. Compliance for flexible printed boards is tied to IPC-6013E Class 3, with final copper peel strength measured at 0.8–1.2 N/mm using the IPC-TM-650 solder float and adhesion test sequence, and dimensional stability controlled to ±0.10% after exposure to 260 °C reflow. Terminal finished product categories include foldable display hinge flex circuits, medical endoscope imaging cables, automotive airbag spiral cables, and rigid-flex battery management interconnects, where the electroless seed layer must retain ≥ 90% of initial adhesion after 10,000 cycles of dynamic bending at 2 mm bend radius.Adoption of mSAP and semi-additive processing for FC-CSP and BGA substrates constrains the electroless copper seed layer to a thickness window that prevents flash-etch widening of final line/space. The working bath is prepared at 16–20 vol% concentrate, with cupric ion concentration held at 2.0–2.8 g/L, sodium hydroxide at 8.0–10.0 g/L, and 37% formaldehyde at 3.0–3.5 mL/L; replenishment for the horizontal electroless copper module is set at 0.10–0.14 L concentrate per 10 m² of processed substrate area, and the bath is changed every 8–10 metal turnover cycles to limit ABF-derived resin bleed and subsequent electrochemical instability. The production sequence comprises laser via drilling in 35–50 μm ABF dielectric, plasma desmear using CF₄/O₂ mixture at 200–300 W RF power for 15–25 min, alkaline permanganate post-desmear, pre-dip, palladium activation, and horizontal electroless copper deposition to 0.30–0.45 μm; after seed layer deposition, photosensitive dry film is laminated and patterned for 10/10 μm to 15/15 μm line/space, followed by pattern copper electroplating and flash etching. Compliance for IC substrates is verified under IPC-6012E for rigid substrate base performance and JIS C 5012 for pad flatness and solder joint reliability, with surface roughness of the deposited seed layer measured at Ra ≤ 0.03 μm and alkali metal contamination on the final substrate surface below 0.5 μg/cm² by ion chromatography. Terminal products are flip-chip chip-scale packages, system-in-package modules, and high-density BGA interposers, where void-free via bottom coverage and controlled thin seed thickness determine package reliability in temperature cycling from -65 °C to 150 °C for 1,000 cycles.
    Comparative Operating Limits by Downstream Segment
    SegmentConcentrate RatiopHHCHOSeed Cu ThicknessDwell Time
    Multilayer rigid PCB18–22 vol%12.5–12.84.5–5.5 mL/L0.35–0.65 μm6–9 min
    HDI microvia12–15 vol%12.3–12.53.0–4.0 mL/L0.25–0.45 μm5–7 min
    Flex and rigid-flex15–18 vol%12.3–12.53.5–4.5 mL/L0.25–0.50 μm5–8 min
    IC substrate16–20 vol%12.3–12.63.0–3.5 mL/L0.30–0.45 μm4–6 min
    Automotive rigid PCB20–25 vol%12.5–12.84.5–6.0 mL/L0.45–0.80 μm10–14 min
    High-frequency laminate14–18 vol%12.3–12.63.0–4.0 mL/L0.25–0.40 μm6–10 min

    When Thermal Cycle Stress Demands Enhanced Electroless Copper-Adhesion in Automotive Powertrain Boards

    Automotive powertrain, ADAS, and battery management board qualification imposes thermal expansion mismatch between the epoxy-glass base material and plated copper, making the electroless copper interface the primary location for corner cracks and barrel fatigue after long-term thermal cycling. The bath is operated at the higher end of the permissible concentration band, 20–25 vol% concentrate in deionized water, with pH 12.5–12.8, sodium hydroxide 9.0–12.0 g/L, formaldehyde 4.5–6.0 mL/L, and cupric copper 2.8–3.5 g/L; a two-stage replenishment program injects 0.25–0.35 L concentrate per 100 m² panel area plus 1.5–2.0 mL stabilizer per liter of replenisher, and the bath is sampled every 4 h for polarographic copper and UV-Vis absorbance at 550 nm to detect additive decomposition. The horizontal line must hold panels at a dwell time of 10–14 min for aspect ratios up to 10:1, with nozzle pressure 0.22–0.28 MPa and an in-line ultrasonic chamber at 38 kHz to dislodge hydrogen bubbles from through-hole interiors; after electroless copper deposition of 0.45–0.80 μm, panels are processed through electrolytic copper plating to a minimum corner thickness of 25 μm and then submitted to thermal stress testing at 288 °C for 10 s per IPC-6012E Class 3, followed by 1,500 cycles of -40 °C to 125 °C thermal shock with electrical resistance change below 10%. Governing compliance includes IATF 16949 process control requirements for the automotive supply chain, RoHS Directive 2011/65/EU, and REACH Regulation (EC) No 1907/2006 Annex XVII restrictions on formaldehyde emissions during the electroless copper operation. Terminal finished parts are engine control modules, transmission-mounted sensor assemblies, radar modules for adaptive cruise control, and battery management unit boards, where the metallization layer must maintain electrical continuity after 2,000 h of high-temperature operating life testing at 105 °C.

    Hydrocarbon-Ceramic Laminate Hole Walls in 5G Base Station and mmWave Radar Fabrication

    High-frequency laminates containing PTFE, hydrocarbon resin, or ceramic-filled thermoset materials present a low-surface-energy, smear-prone hole wall that resists conventional alkaline permanganate treatment and demands plasma desmear plus controlled electroless copper initiation. The working bath concentration is set at 14–18 vol% to moderate the copper deposition rate and prevent over-roughening of the resin matrix, with sodium hydroxide at 7.0–9.0 g/L, formaldehyde at 3.0–4.0 mL/L, and stabilizer additive maintained by capillary analysis at 0.5–0.8 mL/L; the pH is held at 12.3–12.6 to reduce attack on ceramic fillers, and the bath is filtered through 0.5 μm absolute cartridges with continuous carbon adsorption to remove low-molecular-weight PTFE decomposition products. The downstream production route includes plasma desmear in a vacuum chamber with O₂/N₂ ratio 1:1 to 1:3, RF power 500–800 W, and process time 20–40 min, followed by a fluoropolymer-compatible conditioner, palladium activation with strong agitation, and horizontal electroless copper deposition at 30–32 °C for 6–10 min to yield a seed layer of 0.25–0.40 μm; electrolytic copper plating then builds the conductive layer to 18–25 μm for controlled impedance. Industry compliance references IPC-4101D slash sheets for low-loss laminate properties, IPC-6018 for microwave printed board qualification, and RoHS Directive 2011/65/EU Annex II; final hole wall pull-away is inspected by microsectioning after lead-free reflow at 260 °C. Terminal finished products include 5G base station antenna boards, mmWave radar array substrates, satellite communication receive/transmit modules, and high-speed digital test fixtures, where the electroless copper seed must achieve uniform coverage without resin recession exceeding 5 μm.
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    Certification & Compliance
    More Introduction

    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.

    How does horizontal impingement alter through-hole copper distribution compared with vertical processing?

    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.

    Bath composition boundaries and organic additive sensitivity

    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 ion55–75 g/LICP-OES
    Sulfuric acid180–230 g/LAcid-base titration
    Chloride40–70 mg/LPotentiometric titration
    Bath temperature22–28 °CPT100, sump or cell return
    Cathodic current density2.0–3.5 A/dm²Rectifier monitor
    Deposition time for 20 µm10–20 minProcess control, current-density dependent
    Anode typeIr-Ta-coated titanium, insolubleSupplier specification
    Filtration10 µm cartridgesPolypropylene 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.

    When high-aspect-ratio boards above 10:1 enter production, what failure modes become measurable?

    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 thicknessIPC-6012 Class 3≥25 µm average, ≥20 µm minimum wall
    Thermal stress integrityIPC-TM-650 2.6.8No internal cracks or plating separation after 288 °C, 10 s
    Coating thickness measurementASTM B568X-ray fluorescence, calibrated to copper
    Restriction of hazardous substancesDirective 2011/65/EU Annex IINo Pb, Cd, Hg, Cr(VI), PBB, PBDE above limits
    REACH informationRegulation (EC) No 1907/2006 Article 33SVHC disclosure as applicable
    Quality managementISO 9001:2015Lot traceability, certificate of analysis
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