| HS Code | 399694 |
| Productname | PCB Etchant (Guanghua Technology Acidic Etchant) Electronic/EL Grade |
| Grade | Electronic/EL |
| Chemicaltype | Acidic copper chloride etchant solution |
| Chemicalcomposition | CuCl2 + HCl + H2O |
| Cucl2content | Approximately 25-35 wt% |
| Hclcontent | Approximately 10-15 wt% |
| Coppercontent | Approximately 9-12 wt% |
| Chloridecontent | Approximately 18-23 wt% |
| Appearance | Clear liquid |
| Color | Blue-green |
| Odor | Pungent, hydrochloric acid-like |
| Specificgravity20c | 1.20-1.35 |
| Ph | <1 |
| Meltingpoint | Approximately -20°C to -10°C |
| Boilingpoint | Approximately 105-110°C |
| Solubilityinwater | Fully miscible in all proportions |
| Electricalconductivity | High ionic conductivity |
| Etchcharacteristic | Regenerable acidic cupric chloride etch chemistry |
As an accredited PCB Etchant (Guanghua Technology Acidic Etchant) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in a 1 L high-density polyethylene bottle with a secure, leak-proof cap, labeled clearly as Guanghua Technology Acidic Etchant, Electronic/EL Grade. |
| Container Loading (20′ FCL) | 20′ FCL of Guanghua Technology Acidic PCB Etchant (Electronic/EL Grade), packed in sealed containers, palletized, and secured for safe transport. |
| Shipping | Ship as UN3264, “Corrosive liquid, acidic, inorganic, n.o.s.,” Class 8, packaging group per SDS. Use leakproof, corrosion-resistant containers in properly marked outer packaging. Include hazard labels, segregation from bases/oxidizers, upright orientation, and complete DG paperwork with SDS. Electronic/EL grade requires traceability and contamination-free handling. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and incompatible materials like alkalis or reactive metals. Keep the container tightly sealed when not in use, protected from moisture, and clearly labeled. Use corrosion-resistant secondary containment. Ensure adequate ventilation and follow manufacturer’s safety instructions. |
| Shelf Life | Shelf life is typically 12 months when stored unopened in its original container at room temperature, away from direct sunlight. |
In rigid multilayer PCB fabrication, inner-layer patterning uses selective copper removal from epoxy-glass cores before lamination. Guanghua Technology Acidic Etchant, Electronic/EL Grade, is run in horizontal conveyorized spray etchers with titanium or PVC/CPVC wetted parts; Type 316L stainless steel is excluded because chloride pitting initiates within 200–500 h of continuous contact. The control band for the cupric chloride system is typically maintained at 120–180 g/L cupric ion, 150–220 g/L free hydrochloric acid, specific gravity 1.25–1.35, and temperature 48–52 °C. Spray pressure across cone nozzles is held between 0.8 bar and 1.2 bar. Oxidation-reduction potential is controlled at 520–560 mV versus Ag/AgCl; potentials above 580 mV accelerate lateral attack and degrade etch factor, while readings below 500 mV reduce vertical etch rate enough to require longer dwell time and produce rough sidewalls. The primary redox cycle converts metallic copper to cuprous chloride, after which air sparging or metered sodium chlorate regenerates cupric chloride. Free acid is monitored by acid-base titration rather than pH because concentrated chloride media destabilise membrane pH electrodes and produce drift. Cooling coils and heat-exchanged recirculation loops are required to keep the bath temperature within ±2 °C, because etch rate changes by approximately 4–6% per °C in this window.
Breakpoint is maintained at 55–65% of chamber length so that the remaining spray zone acts as a controlled over-etch stage. Dry-film photoresist of 38 µm thickness withstands the acid environment for typical contact times not exceeding 180 s; protective edge erosion is checked after first-article panels. Cross-sectional measurements following ASTM B487-85 quantify vertical etch depth and lateral undercut, and the etch factor for inner-layer traces at 75 µm line pitch is commonly 2.5–3.5. After stripping and automated optical inspection, the cores proceed to brown oxide or black oxide coating and subsequent multilayer stack lamination. Acceptance of conductor width and spacing is referenced to IPC-6012F for Class 3 inner layers, with final qualification also conditioned by IPC-4101E base material requirements. The downstream product is a registered inner-layer core set used in high-layer-count server, telecom, and aerospace multilayer constructions.
Flexible circuit production laminates or deposits 18 µm, 12 µm, or 9 µm copper onto polyimide film, then processes the web through roll-to-roll etchers at 250–520 mm width and 2–8 m/min speed. The etchant temperature is intentionally constrained to 45–50 °C, which is lower than rigid-board ranges, to reduce dimensional movement of the polyimide carrier and to limit hydrochloric acid vapour carry-over into downstream rinse sections. Low trace-cation loading in Electronic/EL Grade is significant for adhesiveless cast-on-polyimide constructions; iron above 1 mg/L can participate in local galvanic cells at the copper-polyimide interface and generate isolated pitting. Free chloride is held at the upper end of 180–220 g/L to maintain cuprous chloride solubility and prevent precipitation on horizontal chamber seals and lip rollers. Web tension is controlled by dancer rolls ahead of the etch chamber; tension variation greater than ±5% causes width change that later appears as misregistration during coverlay or stiffener lamination. Post-etch copper sidewall roughness is typically held between Ra 0.20 µm and Ra 0.30 µm to balance coverlay adhesion against flexural fatigue life. The etched flex core may become a single-sided, double-sided, or multilayer flexible printed circuit used in smartphones, medical catheters, automotive dashboards, and foldable display links. Compliance commonly references IPC-6013D for flexible circuit performance and IPC-4562A for incoming copper foil, with undercut verified by optical cross-section at 400× magnification after first-piece approval.
| Segment | Cu2+ (g/L) | Free HCl (g/L) | ORP (mV vs Ag/AgCl) | Temperature (°C) | Primary control target |
|---|---|---|---|---|---|
| Rigid inner layer | 120–180 | 150–220 | 520–560 | 48–52 | Breakpoint and etch factor |
| Flex roll-to-roll | 110–160 | 180–220 | 530–570 | 45–50 | Web tension and pitting resistance |
| mSAP seed removal | 80–120 | 160–200 | 540–570 | 47–50 | Over-etch allowance |
| Heavy copper | 150–180 | 150–180 | 510–540 | 46–50 | Exotherm and puddle control |
| Controlled impedance | 100–140 | 160–190 | 530–560 | 49–51 | Line width stability |
After pattern plating of a modified semi-additive process (mSAP) or semi-additive process, the exposed copper seed layer is removed without converting the plated circuit profile into a strongly trapezoidal shape. In this step the seed copper is typically 0.5–3 µm thick, while the plated copper feature is 8–18 µm thick. Because the acidic etchant does not chemically distinguish seed copper from plated copper under practical operating conditions, geometric uniformity and short residence time dominate the process. Horizontal flash-etch modules for mSAP use fixed nozzle arrays with 0.5 mm orifice diameters and spray pressure below 0.6 bar to minimise puddling, which otherwise causes preferential etching in narrow spaces. Cupric ion is maintained at 80–120 g/L, free HCl at 160–200 g/L, ORP at 540–570 mV, and temperature at 47–50 °C. The lower copper concentration improves etch uniformity when only a thin seed must be removed. Endpoint is determined by colour change sensors or optical densitometry; an over-etch allowance of 10–20% of seed thickness is typical. Finished HDI boards with line/spacing of 20/20 µm or 15/15 µm then proceed to organic solderability preservative or ENIG surface finish. Cross-sectional verification uses ASTM B487-85, and the dielectric surface between traces is held below Ra 0.25 µm by non-contact profilometry. Acceptance is commonly tied to IPC-6016D for HDI constructions.
Mobile cation control is particularly important because mSAP traces are separated by thin carbon dioxide laser-drilled dielectric and are later subjected to biased humidity testing. Sodium and iron concentrations above 0.5 mg/L can form conductive residues after downstream ENIG or immersion tin processing. Rinse conductivity after etching is therefore monitored and held below 10 µS/cm before panels exit the final cascade. The process is incompatible with brass or bronze fittings in the recirculation loop because cupric chloride attacks copper alloys. End product examples include smartphone mainboards, tablet motherboards, and high-density camera module substrates.
Flip-chip and wire-bond package substrates built on BT or ABF laminates use semi-additive processing. The residual copper seed between pattern-plated traces is removed on horizontal etchers; the acid etchant must produce an etch factor above 4 for line/spacing 12/12 µm and above 6 for 8/8 µm. At these geometries, 1 µm of lateral attack per side consumes a disproportionate share of the conductor width. Electronic/EL Grade low sodium and low iron content is preferred because mobile ion contamination on package substrates can degrade wire-bond adhesion and highly accelerated stress test performance. Free chloride is held at 170–210 g/L, cupric ion at 90–130 g/L, ORP at 530–560 mV, and temperature at 48–50 °C. A closed-loop regeneration circuit injects hydrogen peroxide or sodium chlorate in proportion to copper loading; hydrogen peroxide addition above 3.0 mL/L per regeneration cycle is avoided because hot oxidizer can passivate copper and induce non-uniform flash etch. After etching, the substrate proceeds to desmear, electroless copper, electrolytic copper, and solder mask. End product qualification may include JEDEC JESD22-A110 highly accelerated stress testing and IPC-6016D or IPC-6012F Class 3 acceptance. The final package substrate may be ENEPIG-finished for wire bonding or used as a direct flip-chip pad surface.
One operational boundary is the accumulation of chlorate in low-bleed systems. When sodium chlorate is used as the primary oxidizer and the drag-out rate is small, chlorate can exceed 5 g/L and contribute to resist lifting at the trace edge. Bleed-and-feed or electrolytic copper recovery controls the build-up. The etch bath is also incompatible with elastomer seals containing nitrile rubber; perfluoroelastomer or EPDM seals are required for continuous duty above 1000 h.
Copper thickness above 105 µm on power boards changes the etch process from a short pass to a sustained exothermic reaction. On horizontal equipment, panel temperature may rise 6–10 °C across a single pass when etching 210 µm foil unless the etch sump includes external cooling sized to hold the bath within ±2 °C of setpoint. The etchant is operated at lower ORP, 510–540 mV, and higher cupric ion, 150–180 g/L, to reduce lateral attack while maintaining vertical etch. Free HCl is held at 150–180 g/L; higher acid concentration attacks resist edges and lowers etch factor. Spray bar oscillation at 20–30 cycles/min prevents puddling in dense high-current patterns. End product examples include power converter busbars, IGBT module substrates, motor drive boards, and thermal management layers. After etch, panels are inspected by X-ray thickness measurement for trapped cuprous chloride deposits in narrow gaps. If cuprous chloride precipitates, an immediate acid flush at twice the normal HCl concentration is required before the line stops to prevent solidification in the spray manifold. Acceptance criteria for conductor thickness and width commonly follow IPC-6012F Class 3, with thermal stress test IPC-TM-650 2.6.7 used to validate copper integrity after solder float.
A process limitation with heavy copper is the low throughput relative to thin-foil etching. Conveyor speed for 210 µm copper may be as low as 0.2–0.5 m/min depending on chamber length and nozzle pressure. Rack systems are sometimes preferred over conveyorised units when panel distortion exceeds 0.5% after etching. The bath also accumulates copper quickly; copper concentration must be bled or fed to an electrowinning loop to stay below 180 g/L. If copper rises above that limit, cupric chloride crystallisation can occur in cool zones of the sump and recirculation piping.
Controlled impedance boards used in 5G antenna arrays and automotive radar modules require etched line widths to remain within ±5 µm of the CAM design, because characteristic impedance shifts by roughly 1–2 Ω per 3 µm width change on thin laminates. Etch uniformity therefore becomes more important than absolute etch rate. The acid etchant is run in high-flow vertical spray chambers with 50–100 L/min per nozzle row to create a uniform boundary layer across the panel. ORP is maintained at 530–560 mV with automated oxidizer dosing; cupric ion is held at 100–140 g/L, free HCl at 160–190 g/L, and temperature at 49–51 °C. In-line dimension measurement after resist stripping provides closed-loop adjustment of conveyor speed and spray pressure. The trapezoidal cross-section is minimised by shortening etch time and increasing vertical etch rate, but over-aggressive chemistry attacks the nodular copper surface and raises conductor loss. Post-etch surface roughness is targeted below Ra 0.35 µm. Downstream products include 77 GHz radar antenna boards, low-loss RF modules, and high-speed digital backplanes. Verification references IPC-2221A for conductor width design and IPC-TM-650 2.5.5.7 for impedance, with final single-ended acceptance typically 50 Ω ± 5 Ω.
The process window is narrow when high-frequency laminates are not glass-reinforced or contain low-loss fillers; the etchant can attack exposed filler particles at the sidewall, so spray pressure above 1.0 bar is avoided on such materials. Pre-etch surface preparation must remove chromate or silane treatment from the copper foil; otherwise the breakpoint becomes erratic. Rinse water conductivity below 10 µS/cm is required to prevent ionic contamination on the dielectric, which would shift effective dielectric constant under humidity.
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Guanghua Technology Acidic Etchant, Electronic/EL Grade, is an acidic cupric chloride–hydrochloric acid etching solution formulated for subtractive copper patterning of printed circuit boards. The product is supplied as a liquid concentrate for make-up and replenishment; the working bath contains copper(II) chloride as the primary oxidant, hydrochloric acid, and chloride-ion sources. In the etching reaction, Cu(II) oxidizes metallic copper to Cu(I); the Cu(I) is re-oxidized to Cu(II) by air sparging, chlorine injection, or controlled addition of sodium chlorate/hydrogen peroxide. The Electronic/EL Grade designation corresponds to a controlled trace-metal and particle-quality envelope rather than a single fixed bath composition. Standard production concepts include horizontal conveyorized spray etch chambers with conveyor widths of 600–750 mm, nozzle manifold pressures of 1.5–3.0 bar, and bath temperatures of 45–55 °C. The solution is used for inner-layer etching, outer-layer patterning, and seed-layer removal in semi-additive processing where fine-line performance, resist compatibility, and copper-loading capacity are the main selection criteria. Specific model or lot designations are assigned by the manufacturer for traceability; the Electronic/EL Grade suffix should be referenced on purchase specifications to avoid substitution with standard technical-grade cupric chloride etchants.
Control of free hydrochloric acid, total copper, and chloride addition is the primary chemical mechanism for regulating etch factor. Free hydrochloric acid is normally maintained at 1.5–3.0 mol/L, total copper at 120–180 g/L, and sodium chloride at 180–260 g/L. The chloride-to-copper molar ratio is held above 3.5:1 to prevent precipitation of cuprous chloride, which blocks nozzles and reduces etch uniformity. If the ratio falls below 3.0:1, cuprous chloride film formation on the copper surface increases undercut at the resist edge. Above 5.0:1, bath density and viscosity increase; recirculation energy rises and spray impingement can mechanically lift dry-film resist from fine-line features.
The ORP setpoint is generally 520–580 mV vs Ag/AgCl. Lower ORP slows re-oxidation of Cu(I) and reduces etch rate; higher ORP increases lateral attack beneath the resist. A 5 °C increase in bath temperature can raise etch rate by approximately 10–15% under otherwise unchanged chloride and ORP conditions. Etch factor for conductor widths of 35–50 μm is typically 3.0–5.0 in conventional horizontal spray equipment. Published data for conductor widths below 25 μm with this specific product configuration is limited; qualification on the actual etch line is necessary because nozzle oscillation, conveyor speed, and panel thickness influence etch uniformity to a degree comparable to bath chemistry.
Regeneration chemistry also affects the chloride-to-copper ratio. Air sparging and chlorine injection convert Cu(I) back to Cu(II) without copper removal; the dosing rate must balance Cu(I) generation from the etch reaction. If chlorine is overdosed, free chlorine attacks the resist and increases undercut. Typical chlorine consumption is 0.3–0.5 kg per kilogram of etched copper depending on ventilation and chlorate formation; this value should be monitored by a gas mass-flow meter. Sodium chlorate is an alternative oxidant when chlorine gas storage is not permitted; it introduces sodium ions and increases sodium chloride concentration over time. Hydrogen peroxide is used only in converter systems or with controlled dosing because it can decompose catalytically on copper surfaces and cause local ORP spikes.
| Parameter | Typical range | Analytical method or equipment |
|---|---|---|
| Free hydrochloric acid | 1.5–3.0 mol/L | Acid-base titration with 1.0 N NaOH |
| Total copper | 120–180 g/L | Iodometric titration or atomic absorption spectroscopy |
| Specific gravity at 25 °C | 1.20–1.40 g/cm³ | ASTM D4052 |
| Oxidation-reduction potential | 520–580 mV vs Ag/AgCl | ASTM D1498 |
| Bath temperature | 45–55 °C | PID-controlled titanium or PTFE heater |
| Spray pressure | 1.5–3.0 bar | Manifold pressure transmitter |
| Sodium chloride | 180–260 g/L | Argentometric titration |
Electronic/EL Grade material is filtered to 0.2 μm absolute before packaging; this reduces particle-related defects in fine-line etching. Trace-metal analysis by inductively coupled plasma mass spectrometry (ISO 17294-2) monitors iron, nickel, chromium, cobalt, zinc, and manganese, which can deposit galvanically on copper or shift ORP response. Certificate-of-analysis limits are batch-specific and depend on hydrochloric acid feedstock, container type, and storage duration. The grade does not automatically provide sub-ppb purity; customers requiring cation levels below 50 ppb per element should specify dedicated fluoropolymer or high-density polyethylene packaging, inert-gas blanketing, and single-use containers. Storage at 5–35 °C in closed containers limits iron pickup and chloride fuming. If the working bath accumulates more than 1 mg/L of total transition metals, the ORP signal can shift and dark deposits may appear on copper surfaces after post-etch rinsing.
In a multi-line PCB facility, analytical frequency is usually tied to bath age and panel throughput. Free acid and specific gravity are checked every 2 h during continuous production; ORP is used for real-time dosing. Copper concentration is verified by iodometric titration or atomic absorption spectroscopy at start-up and every 8 h. Chloride concentration is checked daily or after large replenishment events. This monitoring schedule is not a product-specific requirement but reflects the sensitivity of cupric chloride chemistry to copper loading and chloride loss through drag-out. Drag-out losses for horizontal spray lines are generally 50–150 mL/m² of processed panel; this value influences replenishment rates and wastewater treatment load. A closed-loop rinse system with conductivity monitoring reduces chloride discharge and helps maintain a stable bath concentration.
Wetted materials in a production line include polypropylene, polyvinyl chloride, chlorinated polyvinyl chloride, and fiberglass-reinforced plastic. Titanium is restricted to heating elements because cupric chloride solutions passivate titanium under oxidizing conditions but can cause pitting if the ORP falls into reducing conditions. Low-pressure diaphragm pumps or magnetically coupled centrifugal pumps with polypropylene casings are typical; mechanical seals must be selected for hydrochloric acid service. Spray bars with nozzle diameters of 0.8–1.2 mm deliver solution to both sides of the panel; nozzle spacing and oscillation are set to maintain uniform impingement. Conveyor speed is normally 2.0–5.0 m/min; 18 μm copper foil reaches etch breakpoint in approximately 45–90 s depending on ORP and bath temperature.
The chemical control loop uses ORP and specific gravity as input signals; chlorine gas or sodium chlorate is dosed to raise ORP, and hydrochloric acid is dosed to maintain free acidity. Batch-to-batch variance is observed when chloride concentration drifts more than ±5 g/L from the setpoint or when specific gravity control is delayed by density-sensor fouling. This is a common production failure mode in facilities where replenishment is manual rather than flow-proportional; it produces under-etching near the panel center and over-etching at the leading edge. For inner-layer etching of 35 μm copper, a two-stage chamber with different ORP zones can reduce undercut by using a lower ORP in the final breakpoint zone.
Acidic cupric chloride is selected over ferric chloride when copper loading, regeneration, and sludge volume are limiting. Ferric chloride etches copper by Fe(III) reduction to Fe(II) and accumulates iron hydroxide sludge; acidic cupric chloride regenerates Cu(II) by air or chlorine oxidation, allowing continuous operation at a copper concentration of 120–180 g/L. Etch rates at 50 °C for cupric chloride systems are typically 0.8–1.5 μm/min depending on ORP and chloride concentration, whereas ferric chloride may slow as iron content increases. Etch factor for 35–50 μm lines is 3.0–5.0 for acidic cupric chloride and commonly 1.5–2.5 for uninhibited ferric chloride. Compared with alkaline ammoniacal etchants, the acidic product is compatible with most dry-film and liquid photoresists but incompatible with alkali-soluble resists; alkaline systems require ammonia recovery or breakpoint chlorination and may attack certain photoresists. The acidic product is also preferred when downstream wastewater treatment uses electrowinning rather than hydroxide precipitation because copper can be recovered directly without iron contamination. Chlorine regeneration requires gas detectors with alarm thresholds of 1 ppm and fume extraction systems sized for HCl and chlorine; this is a process-safety difference not present with ferric chloride. For fine-line work below 50 μm, the lower viscosity of cupric chloride solutions gives more consistent nozzle coverage and reduces spray shadowing at dense conductor arrays. Copper recovery by electrowinning from acidic cupric chloride uses insoluble anodes at cathode current densities of 2–4 A/dm², returning copper cathode scrap and liberating chloride for bath reuse. Published data for the specific Guanghua Technology product under modified semi-additive processing with flash-etched seed layers is limited.
| Characteristic | Acidic cupric chloride | Ferric chloride | Alkaline ammoniacal |
|---|---|---|---|
| Oxidant regeneration | Air or chlorine oxidation of Cu(I) | Limited; iron sludge disposal | Air regeneration of cuprous complex |
| Typical etch factor for 35–50 μm lines | 3.0–5.0 | 1.5–2.5 | 3.0–4.0 |
| Copper capacity | 120–180 g/L | 60–100 g/L before sludge removal | 140–170 g/L |
| Resist compatibility | Most dry-film and liquid photoresists | Most dry-film; some liquid resists degraded by iron | Not suitable for alkali-soluble resists |
| Waste treatment burden | Copper recovery by electrowinning or precipitation | Iron and copper hydroxide sludge | Ammonia recovery or breakpoint chlorination |
Operational boundaries for the Electronic/EL Grade are set by resist compatibility, materials of construction, and rinse-water ionic cleanliness. The working bath must not be mixed with ammonia or alkaline cleaners; neutralization releases heat and precipitates copper hydroxide. Mixing with strong reducing agents can generate hydrogen chloride vapor, and uncontrolled addition of hydrogen peroxide in the presence of chloride can produce chlorine gas. The solution is corrosive to carbon steel, galvanized steel, and most stainless steel; Schedule 40 stainless steel pipe may fail within 72 h under continuous exposure. Exhaust ventilation should maintain workplace concentrations below the ACGIH TLV-TWA limits of 2 ppm for hydrogen chloride and 0.5 ppm for chlorine; local regulations may impose lower ceilings. Post-etch rinsing with deionized water is required to reduce chloride residues that can cause electrochemical migration. The final conductor width, copper thickness, and undercut should be verified against IPC-6012 inspection criteria on production panels. Because published data for this specific grade under low-cupric ion regimes is limited, qualification trials for a new bath should include at least 30 panels across 3 independent bath make-ups and should include thermal-humidity bias testing of soldermask adhesion and surface insulation resistance.