| HS Code | 332072 |
| Productname | Copper Plating Solution (MacDermid MacuSpec HT-300) Electronic/EL Grade |
| Manufacturer | MacDermid Enthone |
| Producttype | Acid copper electroplating solution |
| Grade | Electronic/EL Grade |
| Appearance | Clear, deep blue liquid |
| Physicalstate | Liquid |
| Odor | Slight acidic odor |
| Chemistry | Copper sulfate, sulfuric acid, chloride ions, and proprietary organic additives |
| Specificgravity | 1.10 to 1.18 at 25°C |
| Ph | <1 |
| Copperconcentration | Approximately 15 to 25 g/L as Cu |
| Sulfuricacidconcentration | Approximately 180 to 230 g/L |
| Chlorideconcentration | Approximately 50 to 100 mg/L (ppm) |
| Watersolubility | Fully miscible/soluble in water |
| Boilingpoint | Approximately 100°C (aqueous solution) |
| Purity | Low trace-metal content, suitable for electronic/EL applications |
| Storagetemperature | 15 to 30°C |
| Shelflife | Typically 6 months when stored sealed in original container |
As an accredited Copper Plating Solution (MacDermid MacuSpec HT-300) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Copper Plating Solution (MacDermid MacuSpec HT-300) Electronic/EL Grade, 1 L, supplied in a sealed HDPE bottle with clear hazard and batch labeling. |
| Container Loading (20′ FCL) | 20′ FCL: Copper Plating Solution (MacDermid MacuSpec HT-300, EL grade) in UN-approved drums, palletized, secured, labeled Class 8 corrosive. |
| Shipping | Shipping description: **UN 1760, Corrosive liquids, n.o.s. (contains sulfuric acid), Class 8, Packing Group II** for Copper Plating Solution (MacDermid MacuSpec HT-300) Electronic/EL Grade. Transport in leak-tight, compatible containers, kept upright and segregated from alkalis/cyanides. Mark packages with the standard corrosive and UN identification labels. |
| Storage | Store in tightly sealed original containers in a cool, dry, well-ventilated area away from direct sunlight, heat, and incompatible materials. Keep temperature stable and above freezing. Use secondary containment to prevent leaks. Ensure containers are clearly labeled and accessible for inspection. Follow manufacturer’s guidelines and local regulations for electronic/EL grade handling. |
| Shelf Life | Shelf life is typically 12 months from manufacture date when stored unopened at room temperature in original container, protected from freezing and contamination. |
MacuSpec HT-300 acid copper electrolyte is introduced into the process sequence after electroless copper deposition of 0.3–0.8 µm on desmeared high-Tg FR-4, halogen-free FR-4, or polyimide laminates. Vertical continuous plating equipment for backplane panels uses phosphorized copper anodes with phosphorus content 0.04–0.06 wt% held in titanium anode baskets, polypropylene tanks rated for continuous exposure at 60–70 °C, and filter cartridges with 1–5 µm absolute retention. The working bath maintains CuSO4·5H2O at 60–100 g/L, H2SO4 at 180–220 g/L, chloride ion at 40–80 ppm, and organic suppressor–brightener–leveler components metered by ampere-hour replenishment. Cathode current density is set between 1.0 A/dm² and 2.5 A/dm², with electrolyte temperature 20–26 °C and air agitation sufficient to prevent localised Cu2+ depletion at the hole mouth. Deposit thickness in cross-section is measured on polished coupons per IPC-TM-650 2.1.1 and ASTM B487-20; for IPC-6012 Class 3 boards, the barrel copper thickness is evaluated against the minimum requirement for the relevant dielectric type and layer count.
Table 1 — Operating envelope for electronic-grade acid copper used in vertical continuous plating of MacuSpec HT-300
| Parameter | Range | Unit |
|---|---|---|
| CuSO4·5H2O | 60–100 | g/L |
| H2SO4 | 180–220 | g/L |
| Chloride ion | 40–80 | ppm |
| Bath temperature | 20–26 | °C |
| Cathode current density | 1.0–2.5 | A/dm² |
| Anode current density | 0.5–1.5 | A/dm² |
| Filtration retention | 1–5 | µm absolute |
| Phosphorized anode phosphorus | 0.04–0.06 | wt% |
In high-aspect-ratio backplane structures, the dominant failure mode is hourglass plating in which the hole-centre deposit is thinner than the surface deposit because of mass-transport limitation and suppressor consumption. Throwing power is therefore monitored as the ratio of hole-centre copper thickness to surface copper thickness; for a 10:1 aspect ratio, high-throwing electronic-grade acid copper processes are expected to maintain a ratio not lower than 0.80 when leveler concentration remains inside its supplier-defined upper control limit. Production experience shows that anode sludging from non-phosphorized copper or broken anode bag seals increases particulate co-deposit and leads to nodulation; routine Hull cell panels at 2 A for 20 min are used to detect brightener imbalance before panel lots are committed. Thermal stress testing at 288 °C for 10 s and subsequent microsectioning per IPC-6012 reveal barrel corner cracks when deposit elongation is inadequate or when the imbalanced organic additive package embeds occluded material at the knee of the hole.
On HDI boards with laser-drilled blind microvias of 40–100 µm top diameter and 60–100 µm dielectric depth, the MacuSpec HT-300 bath is operated to produce bottom-up fill rather than conformal sidewall growth. The leveler component adsorbs preferentially at the via mouth and surface plane, suppressing copper deposition on the top surface while the via bottom remains electrochemically active. For this segment, cathode current density is normally limited to 1.5–2.0 A/dm² because higher current density produces rim nodules at the via mouth and accelerates leveler breakdown, while lower current density prolongs deposition time and yields surface copper below the 10–18 µm target after planarization. Filled vias are evaluated by cross-section at 500×–1000× magnification; void area below 5% of via cross-section and dimple depth below 15 µm are common acceptance limits on procurement drawings governed by IPC-6016. The deposit must also survive interconnect stress test or thermal cycling from -40 °C to 125 °C without separation at the target pad interface.
Shared use of the same electrolyte for through-hole and blind-via fill creates a secondary process conflict. Organic breakdown products from high-current-density operation accumulate in the bath and compete with the leveler for adsorption sites; failure to maintain dummy plating at 0.2–0.5 A/dm² or to perform selective carbon treatment reduces bottom-up differential, producing centre seam voids and excessive dimple. Hull cell bright-range evaluation at 2 A for 20 min is used alongside cyclic voltammetric stripping of organic deposits to track suppressor/leveler balance. Thermal stress tests on HDI coupons per IPC-6016 and IPC-TM-650 2.1.1 cross-sections identify the transition from acceptable fill to void-opening failure when dimple depth exceeds the design limit and surface copper is too thin to survive etch removal during differential etching.
Flexible polyimide circuits using rolled-copper or electrodeposited foils with thickness 12.5–50 µm present a non-uniform primary current distribution because the thin copper layer itself acts as a resistive electrode during electroplating. MacuSpec HT-300 is operated in reel-to-reel or panel plate equipment at lower current density, commonly 0.5–1.5 A/dm², to reduce burning at via rims and to allow copper deposition into through-holes of 100–300 µm diameter without overplating the flexible surface excessively. Free-standing plated copper deposited from the bath is tested per IPC-TM-650 2.4.18 for elongation and tensile strength; elongation above 12% and tensile strength in the range of 250–400 MPa are typical acceptance values for dynamic flex applications, although the final value is influenced by leveler concentration and deposit grain structure. Thickness distribution across a 250 mm wide flex panel is measured by X-ray fluorescence per ASTM B568-21 at nine positions; a total range below 1.5 µm on a 20 µm target is commonly specified to maintain dimensional stability.
Thermal reliability in flex PTH is limited by differences in the coefficient of thermal expansion between the polyimide substrate, the copper barrel, and the plated surface copper. Plated copper with high elongation and low internal stress resists barrel cracking during thermal shock from -55 °C to 125 °C, but the process window narrows when flex panels are run on the same line as rigid backplanes because the optimum leveler concentration for high throwing power in rigid boards may produce higher stress in flex deposits. Control of chloride at 40–80 ppm is particularly critical because chloride deficiency produces rough, high-stress deposits at the via rim, while excess chloride suppresses brightener action and reduces leveler adsorption. Production data for this specific MacuSpec HT-300 configuration is limited, so the current density and additive concentrations for each flex stack are qualified by cross-section after thermal shock per IPC-6013 and IPC-TM-650 2.1.1.
Semi-additive processing on ABF or BT package substrates uses thin electroless copper seed layers of 0.1–0.5 µm over 510×515 mm panels. MacuSpec HT-300 fills blind vias and plates line-and-space features in the same step, but the resistance of the thin seed layer creates a terminal effect that concentrates current at the panel edge and around isolated features. To limit total thickness variation, current density is held at 0.8–1.5 A/dm² with segmented anodes and edge shielding adjusted to the panel pattern density. Copper thickness on resist-defined traces is measured on a 9-point panel grid by X-ray fluorescence per ASTM B568-21; for a 10 µm target, total range below 1.2 µm and standard deviation below 0.4 µm are common statistical process control limits.
Via filling in package substrates demands bottom-up differential, but the absence of a separate patterned leveler operation means the same electrolyte must balance trace plating uniformity and blind via fill. Cross-sections at 1000× are inspected for seam voids at the via centre and for dimple depth; conformal growth is characterised by the sidewall-to-base copper thickness ratio, with values above 1.3 indicating inadequate leveler adsorption or organic breakdown. The deposit is aged with thermal cycling from -55 °C to 125 °C per JEDEC JESD22-A104 and inspected for via-bottom separation after 500 cycles. Failure analysis of plated through-holes on package substrates shows that current crowding at the via edge produces local grain refinement and higher impurity incorporation; controlling anode-to-cathode spacing and flow velocity at 1–3 m/s across the panel mitigates this effect.
Table 2 — Test standards and measurement methods referenced across downstream segments
| Segment | Standard | Measurement method |
|---|---|---|
| Rigid PTH | IPC-6012 | IPC-TM-650 2.1.1, ASTM B487-20 |
| HDI blind via | IPC-6016 | IPC-TM-650 2.1.1, ASTM B568-21 |
| Flex PTH | IPC-6013 | IPC-TM-650 2.4.18, ASTM B568-21 |
| IC package substrate | JEDEC JESD22-A104 | ASTM B568-21 |
| Ceramic module | ASTM B975-20 | ASTM D3359 |
Concurrently with advanced packaging substrates, high-density interconnect boards for automotive radar and camera modules push the same electrolyte into mixed-via designs where blind via fill, through-hole plating, and fine-line pattern plating occur in one wet-to-wet sequence. In such mixed-mode panels, the dominant process conflict is between the high leveler concentration required for blind via bottom-up fill and the low internal stress required for through-hole thermal cycling. MacuSpec HT-300 is therefore run at an intermediate current density of 1.2–1.8 A/dm², with chloride held near the centre of the 40–80 ppm window. Copper thickness after flash etching is measured by X-ray fluorescence per ASTM B568-21 on a 12-point panel grid; total range is maintained below 1.8 µm for a nominal 20 µm surface copper target. Microsections per IPC-TM-650 2.1.1 are evaluated for hole-centre thickness, blind via void area, and trace sidewall integrity simultaneously.
Field reliability data for automotive high-density interconnect boards indicates that mixed-via designs fail first at the interface between blind via fill and the next lamination cycle when dimple depth or void area exceeds the specified limit. Thermal shock testing from -40 °C to 150 °C with 1000 cycles separates robust bottom-up fill from marginal conformal growth; seam voids open and propagate along the via centre after repeated expansion if the deposit contains incorporated organic films. Bath maintenance is adjusted by dummy plating at 0.2–0.5 A/dm² and total organic carbon tracking; when TOC rises above the supplier-defined upper control limit, leveler adsorption shifts and via fill quality degrades. In this segment, published data for the specific MacuSpec HT-300 mixed-via operating envelope remains limited, and qualification is performed on a product-by-product basis.
Ceramic substrates based on Al2O3, AlN, or Si3N4 are metallised with thin PVD or electroless copper seed layers before MacuSpec HT-300 electroplating builds conductive traces and thermal pads to thicknesses of 20–100 µm. The primary technical requirement in this segment is not throwing power but internal deposit stress, because tensile stress above the ceramic fracture threshold causes microcracks that degrade thermal resistance and RF insertion loss. Stress is measured on deposits plated onto split-strip test coupons per ASTM B975-20; low-stress electronic copper maintained below 10 MPa tensile is typical for ceramic module processing, though the actual value depends on leveler concentration, current density, and bath ageing. Plating is run at 0.5–2.0 A/dm² and 20–26 °C in fountain or paddle cells with continuous filtration at 1–5 µm absolute. Thickness distribution on panels up to 200×200 mm is checked by X-ray fluorescence per ASTM B568-21.
Adhesion to the seed layer and freedom from particulate co-deposit are evaluated by tape test per ASTM D3359 or by cross-section inspection per IPC-TM-650 2.1.1; in RF applications, a single embedded particle larger than 5 µm can create an impedance discontinuity that is detected by time-domain reflectometry. For plated copper on ceramic power modules, thermal cycling from -40 °C to 150 °C is combined with die attachment and wire bonding operations; deposit grain structure must remain stable during subsequent sintering or soldering at temperatures above 250 °C. If organic additives are not maintained at the low-stress setpoint, the deposit hardness increases and may reduce wire-bondability; process control therefore uses Hull cell panels at 2 A for 20 min to confirm the bright-to-matte transition range before high-volume plating. Published data for MacuSpec HT-300 on Si3N4 substrates with direct-bond copper interconnect is limited, and qualification is typically confined to the specific seed metal stack in use.
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MacDermid MacuSpec HT-300 Electronic/EL Grade copper plating solution is a sulfuric acid–based electrolytic copper electrolyte formulated for printed circuit board metallization, including panel plating and pattern plating of through-holes, blind microvias, and high-aspect-ratio multilayer interconnects. The “Electronic/EL Grade” designation indicates a controlled impurity profile intended for electronic interconnect applications in which metallic and organic contamination can influence deposit conductivity, ductility, and thermal cycling reliability. The process is a multi-component system that combines a copper sulfate/sulfuric acid base electrolyte, chloride ion, and organic suppressor, brightener, and leveler additives. The electrolyte operates on a conductive seed layer, typically electroless copper or a flash copper strike, and is differentiated from generic acid copper formulations by its additive package and process control requirements for high throw in low-current-density regions.
Electrochemical operation is governed by copper reduction at the cathode and copper dissolution at the anode. The theoretical deposition rate of copper at 1.0 A/dm² and 100% current efficiency is approximately 0.22 µm/min. Actual production rates are lower when current efficiency is reduced by additive adsorption, anode film changes, or mass-transport limitations in recessed geometries. Current distribution across a patterned panel is nonuniform because the applied cell voltage drops across the electrolyte resistance. Recessed through-hole centres are low-current-density zones, while surface pad edges and high-density outer-layer regions are high-current-density zones. MacuSpec HT-300’s suppressor increases cathode polarization in high-current-density regions, shifting the effective current distribution toward the hole interior. The leveler adds further inhibition at protrusions. This additive-controlled polarization is not equivalent to geometric throwing power; even a high-throw bath cannot compensate for insufficient solution exchange in very small holes.
The base electrolyte functions as a conductive copper ion reservoir. Representative electronic-grade acid copper sulfate ranges include copper metal at 50–70 g/L, sulfuric acid at 180–220 g/L, and chloride ion at 40–80 mg/L. These ranges are deliberately generic for the class; the MacuSpec HT-300 supplier specification may impose tighter limits. Copper sulfate supplies the reducible cupric ion. Sulfuric acid lowers electrolyte resistivity, maintains anode dissolution, and prevents precipitation of basic copper salts. Chloride ion modifies the adsorption of organic suppressors and influences anode polarization; without chloride, the deposit becomes rough and the brightener response decreases.
The organic additive package determines the practical current density window. The suppressor, often a polyether, adsorbs on the cathode surface and increases polarization in high-current-density regions. The brightener, typically a sulfur-containing organic, accelerates electron transfer and refines grain size. A leveler, often a nitrogen-containing compound, adsorbs preferentially on protrusions and reduces step height. The balance among these additives is process-specific. In MacuSpec HT-300, additive concentrations are controlled by cyclic voltammetric stripping analysis and Hull cell panels, not solely by volume additions, because breakdown products alter the electrochemical response without changing copper or acid concentrations.
Production-scale analytical control is required at intervals determined by amp-hour throughput. Hull cell panels are plated at 2 A for 5 min to evaluate bright range, burning, and low-current-density hazing. Cyclic voltammetric stripping analysis quantifies active suppressor, brightener, and leveler concentrations by measuring the stripping charge associated with copper deposition and stripping on a rotating platinum electrode. Titration of copper and sulfuric acid is conducted at minimum once per shift in high-volume installations; chloride is quantified by argentometric or turbidimetric methods. Air agitation or eductor flow is typically maintained to provide uniform solution movement across the panel, but excessive agitation can increase additive consumption and generate foam.
Deposit thickness uniformity is evaluated by cross-sectional measurement according to ASTM B487-20 or an equivalent microsection procedure. For high-aspect-ratio through-holes, the acceptable ratio of through-hole centre copper thickness to surface copper thickness is specified by the board qualification document, often in the range 0.8–1.0 for reliability classes requiring continuous metallic barrel coverage. Leveling is assessed by profilometry or microsection of a defined scratch pattern; the reduction in step height after plating is a function of brightener concentration, current density, and solution agitation. Ductility and tensile strength of the deposited copper should be verified by the foil tensile method described in IPC-TM-650 2.4.18 or by a board-specific method. Published data for this specific configuration is limited, so qualification panels should be generated on the intended line.
Thermal stress testing of plated through-holes is commonly performed by the solder float method of IPC-TM-650 2.6.8 with a float temperature of 288 °C and a 10 s dwell. Copper deposits with high organic inclusion or poor columnar-to-equiaxed transitions may exhibit corner cracks or barrel cracks after the float. Baths with insufficient chloride or degraded leveler often produce low-ductility deposits that pass visual inspection but fail after accelerated thermal cycling. MacuSpec HT-300 is positioned for high-throw acid copper service in such reliability-sensitive applications; however, the specific cycle count obtained depends on the base laminate, plated thickness, and hole geometry.
Chloride ion concentration is a critical control variable because it interacts with the organic suppressor at both anode and cathode. At chloride levels below the supplier lower limit, suppressor adsorption decreases, resulting in rough deposits and increased burning in high-current-density areas. At chloride levels above the upper limit, anode polarization can rise and cuprous chloride films may form on the anode surface, generating sludge and reducing bath life. In high-volume lines, chloride is therefore measured every 4–8 operating hours. Drag-out and drag-in from chloride-containing cleaners or pre-dip solutions must be controlled by cascade rinsing and conductivity monitoring.
Organic additive degradation produces electrochemically active species that can increase deposit stress and reduce soldering wetting. Side-stream carbon treatment is used to remove breakdown products, but excessive carbon treatment can strip essential brightener and leveler components. In MacuSpec HT-300 installations, the regeneration schedule is determined by ampere-hours of production, Hull cell results, and CVS response. The bath should not be operated at uncontrolled high temperature for extended periods because accelerator consumption and brightener decomposition accelerate above 30 °C in representative acid copper formulations.
Through-hole plating quality depends on the interaction between the electrolyte’s throwing power and the panel transport conditions. For holes with aspect ratios above 8:1, solution exchange inside the barrel becomes a rate-limiting step. The MacuSpec HT-300 additive package is intended to maintain suppressor activity in low-current-density regions while allowing acceptable copper thickness at the knee without excessive surface overplate. Qualification microsections should include the smallest plated via diameter and the thickest board processed on the line, because both geometry and racking density influence the actual hole-to-surface thickness ratio.
The difference between MacuSpec HT-300 and conventional bright acid copper appears primarily in the throwing power and leveling balance, not in the base chemistry. Where an incumbent acid copper bath produces a dogboned barrel with thick surface copper and thin centre coverage, a high-throw formulation may produce a more uniform deposit due to stronger suppression in high-current-density regions. This effect is not absolute; it is masked or amplified by current density, board pattern, solution flow, and additive age. Comparative evaluation should therefore be performed on production boards rather than on generic test coupons.
| Chemistry | Operating environment | Throwing power characteristics | Representative cathode current density or thickness | Waste treatment requirement |
|---|---|---|---|---|
| Acid copper sulfate, including MacuSpec HT-300 class | Acidic; requires conductive seed layer | High throw with optimized suppressor/brightener/leveler package; deposit quality dependent on chloride and additive balance | 1.0–3.0 A/dm² | Neutralization, copper recovery, controlled sludge disposal |
| Cyanide copper | Alkaline; can deposit directly on steel and copper alloys | High covering power at low current density; risk of hydrogen embrittlement; fine-grained strike deposits | 0.5–2.0 A/dm² | Alkaline chlorination or peroxide oxidation for cyanide destruction |
| Pyrophosphate copper | Alkaline complexed; requires clean active substrate | Moderate throwing power; sensitive to orthophosphate buildup and organic contamination | 1.0–4.0 A/dm² | Phosphate precipitation, chelator management |
| Electroless copper | Autocatalytic; no external current; deposits on catalyzed nonconductors | Conformal; thickness limited by bath stability and solution exchange | Typical thickness 0.5–1.5 µm | Formaldehyde/hypophosphite and chelator waste treatment |
MacuSpec HT-300 differs from cyanide and pyrophosphate chemistries principally in its acidic operating environment, higher practical current density, and simpler waste treatment. It differs from electroless copper in that it is an electrolytic process requiring a conductive seed layer; it is therefore used for bulk copper buildup rather than initial metallization of nonconductive surfaces. Within the MacuSpec family, supplier technical literature positions HT-300 as a high-throwing-power variant; comparative Hull cell bright range and hole-to-surface thickness ratios should be obtained from the manufacturer for a qualified comparison against other MacuSpec formulations.
Plating line control includes copper and sulfuric acid titrations, chloride determination, Hull cell testing, CVS analysis, and periodic microsection verification. Anode maintenance is equally important. Phosphorized copper anodes with phosphorus content in the range 0.03–0.08 wt% are commonly used to stabilize the anode film and minimize copper particle generation. Anode bags of polypropylene or napped polypropylene are installed to contain sludge. Anode-to-cathode area ratio is typically maintained in the range 1.5:1–2.0:1 in acid copper processes. Filtration through 1–5 µm media is continuous; filters are replaced before differential pressure reaches the supplier maximum.
Tank and auxiliary equipment materials are limited by the acidic, oxidizing environment. Polypropylene, PVC, and CPVC are commonly used for process tanks and risers; carbon steel, aluminum, and unlined stainless steel are incompatible. Heating or cooling is provided by Teflon or quartz heaters and heat exchangers. Rectifier ripple should be limited to less than 5% RMS to reduce nodulation, particularly at high current density. Air agitation is supplied by low-pressure blowers through a sparger manifold; air flow must be uniform and free of oil mist. In horizontal lines, eductor nozzles and flooded cells improve solution exchange in blind microvias.
For qualification, a multiline production trial should include a panel matrix covering minimum, nominal, and maximum current density; microsections of the smallest via diameter; solder shock per IPC-TM-650 2.6.8; and thickness distribution by X-ray fluorescence or cross-section. The resulting data set, rather than supplier general literature, determines whether MacuSpec HT-300 replaces an incumbent electrolyte on a given line.