| HS Code | 230203 |
| Productname | Film Stripping Solution (DuPont EKC-265) Electronic/EL Grade |
| Grade | Electronic/EL Grade |
| Appearance | Clear colorless to slightly yellowish liquid |
| Chemicalcomposition | Mixture of hydroxylamine, 2-(2-aminoethoxy)ethanol, and corrosion inhibitors |
| Solubility | Fully miscible with water |
| Density | Approximately 1.05 g/cm3 at 20°C |
| Ph | Alkaline, approximately 10-11 |
| Primaryfunction | Strips positive photoresist and removes post-etch residues from semiconductor substrates |
| Substratecompatibility | Compatible with silicon-based wafers and various metals used in wafer fabrication |
| Puritylevel | High-purity electronic grade with low metallic and particulate contamination |
As an accredited Film Stripping Solution (DuPont EKC-265) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 1-gallon (3.78 L) high-density polyethylene containers with secure, tightly sealed closures and clear electronic/EL grade labeling. |
| Container Loading (20′ FCL) | 20′ FCL loading of Film Stripping Solution (EKC-265): secure drums/containers, ensure compatibility, ventilate, prevent leakage, avoid direct sunlight, follow hazardous chemical protocols. |
| Shipping | DuPont EKC-265 Film Stripping Solution, Electronic/EL Grade, is a high-purity chemical used to remove photoresist and residue from semiconductor wafers. It should be shipped in clean, leak-proof, compatible containers with proper labeling and hazardous-materials documentation. Exact UN number, hazard class, and packing group must be verified from the product’s current Safety Data Sheet. |
| Storage | Store Film Stripping Solution (DuPont EKC-265) in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight and incompatible materials such as strong oxidizers. Avoid exposure to moisture, heat, and ignition sources. Ensure the container is properly labelled and protected from physical damage. Follow SDS-specific requirements. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored tightly sealed in original container at recommended temperature. |
In wafer-level packaging lines producing copper pillar bumps, positive-tone DNQ-novolac resists with film thickness between 40 µm and 120 µm are applied by spin coating, soft-baked, exposed, and then used as plating moulds for electroplated copper pillars of 25–50 µm height. The resist shell after copper plating is chemically cross-linked at its outermost surface by contact with the acidic copper sulphate or copper methanesulfonate bath. Strip is executed in an exhausted automated wet bench fitted with dual-frequency megasonic transducers at 40 kHz and 1.0 MHz; power density is mapped to 0.5–1.5 W/cm² across the wafer carrier. The bath is charged with undiluted EKC-265 because the corrosion inhibitor package is balanced for the supplied solvent-water equilibrium. Site-specific trials have demonstrated that adding more than 5% deionized water to compensate evaporative loss can shift the copper etch rate above the 1 Å/min acceptance limit during a 60-minute exposed-pad exposure. The standard sequence is two immersion stages of 15–25 minutes each at 65–75 °C, with a nitrogen-bubbled overflow rinse vessel between stages to remove dissolved novolac drag-out. Endpoint is confirmed by automated optical microscopy at 200× magnification and, for released lots, scanning electron microscopy on 10 pillars per wafer at 10 kV accelerating voltage. The acceptance criterion is sidewall residue of less than 0.1 µm² per pillar. The cleaned copper pillars then proceed to SnAg cap deposition and reflow; organic residue on the pillar sidewall creates a non-wetting region during solder reflow and appears as a void in CSAM after moulding.
Stripping of 20–60 µm positive resist from wafers that have completed SnAg solder bump reflow is constrained by tin oxide dissolution and the exposure of aluminium I/O pads. The reflow temperature of 240–260 °C partially carbonizes the resist at the bump interface and forms a graphitic shell that resists simple solvent swelling. Immersion in heated EKC-265 at 70–80 °C for 20–30 minutes penetrates the carbonized crust only when megasonic agitation is maintained at 0.8–1.2 W/cm²; without megasonic energy, comparable thickness can require more than 60 minutes. The extended exposure depletes the aluminium pad thickness budget of 0.8–1.2 µm; pad thinning is measured by stylus profilometry after strip and compared with pre-strip baseline. Aluminium corrosion is suppressed by the inhibitor system, but the inhibition margin narrows as dissolved carbon in the bath exceeds 150 g/L. Above this level, qualification lots should include an electrochemical immersion test on 99.5% aluminium foil per ASTM G1-03, with a maximum accepted mass loss of 0.5 mg/cm² over 30 minutes. A further clearance issue occurs when the post-strip rinse is delayed beyond 60 seconds after the wafer cassette exits the hot stripper; evaporative cooling deposits a viscous amine film on the bump surface. The first rinse uses DI water at 50–60 °C and 18 MΩ·cm resistivity, followed by an isopropanol spray at 0.5–1.0 MPa to remove droplets trapped under 40–60 µm tall bumps. Final inspection is performed by dark-field automated optical inspection; the release limit is typically 5 residue-related defects per 300 mm wafer.
Redistribution-layer processing uses thin positive resists of 5–15 µm to define electroplated copper lines of 2–5 µm width and 5–8 µm thickness over polyimide or silicon-oxide passivation. The stripper is applied in a full-wafer cassette bath or in a single-wafer spray chamber; the bath configuration uses a recirculation pump rated at 20–30 L/min and 0.2 µm PTFE filtration to control polymer gel particles. The rate-limiting step is not bulk dissolution but penetration of the stripper into the resist foot between the copper sidewall and the passivation, which is 0.2–0.8 µm wide after seed-layer etch. A two-stage thermal profile is used: the first 5 minutes at 65 °C swells the resist; the following 8–12 minutes at 75 °C dissolves the released fragments. If the second stage exceeds 15 minutes, atomic force microscopy on 10 µm scan windows shows copper line edge roughness above 0.3 µm RMS, because the stripper begins to attack the copper seed-layer interface. Rinse is a three-step sequence of ambient DI water, hot DI water at 55 °C, and nitrogen blow-off at 0.2 MPa. Final rinse water is monitored for pH and total organic carbon; release limits are derived from ASTM D5127-13 water quality guidelines and are typically set at 50 ppb TOC per wafer. The completed RDL wafer is tested by four-point probe; any residue bridging between 5 µm pitch copper lines lowers measured isolation resistance below 1×10⁹ Ω and fails the wafer-level test map.
| Strip scenario | Film thickness or via depth | Bath temperature | Agitation or flow | Verification method |
|---|---|---|---|---|
| Copper pillar WLP | 40–120 µm | 65–75 °C | 0.5–1.5 W/cm² dual-frequency megasonic | SEM at 10 kV |
| RDL | 5–15 µm | 65–75 °C | 20–30 L/min recirculation | AFM line roughness |
| Fan-out panel | 30–80 µm | 70–78 °C | 0.4–0.8 W/cm² ultrasonic | ASTM D445-21 |
| TSV via plug | 50–100 µm via depth | 65–75 °C two-bath | 40 kHz / 1.0 MHz | Cross-section SEM |
On fan-out panel lines, dry-film stripping imposes a different boundary-layer profile from round-wafer processing. Dry-film resists of 30–80 µm are laminated on 520 mm × 610 mm reconstituted panels and used as plating masks for copper redistribution conductors. The panel format produces lower fluid velocity at the panel corners; resist removal time on corner dies is 2–3× longer than at the centre. A vertical batch stripper with 40 kHz ultrasonic transducers along both sidewalls is operated at 70–78 °C. The transducer power density is limited to 0.4–0.8 W/cm² because higher levels have caused panel warpage and delamination at the moulding compound edge. EKC-265 is charged at 100% as supplied; evaporated solvent is replenished with fresh solution rather than water to maintain inhibitor concentration. The bath is sampled every 4 hours. Kinematic viscosity measured by ASTM D445-21 is used as a surrogate for dissolved dry-film loading; new-bath values are typically 4–6 mm²/s, and the warning limit is 2× the new-bath value. The transfer from strip bath to rinse tank is completed within 45 seconds to prevent edge residues from drying. The rinse protocol uses two counterflow DI water tanks at 45 °C followed by air-knife blow-off at 0.3 MPa. After drying, the panels move to moulding and ball placement; terminal products include fan-out wafer-level application processors and power-management packages.
The exposed aluminium pad on a mixed-metallization bump wafer is the primary compatibility constraint for an alkaline stripper. In the EKC-265 process, aluminium etch rate is a function of bath temperature, water content, dissolved resist concentration, and inhibitor depletion after repeated evaporation cycles. Coupon testing per ASTM G1-03 on 99.5% aluminium is performed at 70 °C and 80 °C for 30 minutes; the pass/fail limit is commonly set at 0.3 mg/cm² per 30 minutes at 70 °C, although the exact acceptance boundary varies by device pad metallization. Published data for the exact EKC-265 aluminium etch rate on mixed-metallization test structures is limited; each line is therefore required to maintain its own coupon baseline before first lot release. Stripping time for 50 µm resist is bounded by incomplete residue clearance at the low end and aluminium pad thinning at the high end. In a 200 mm wafer line with 90-minute bath turnover cycles, the aluminium etch rate can drift from 0.1 µm/hour to above 0.5 µm/hour when the bath is replenished with deionized water rather than formulated solvent. This shift corresponds to a change in the solvent-water azeotrope and depletion of the corrosion inhibitor at the metal surface. Open-circuit potential measurements in a three-electrode cell with a saturated calomel reference electrode monitor inhibitor effectiveness; a shift above +150 mV within 10 minutes indicates the pad has transitioned from passive to active dissolution. Post-strip SEM at 5 kV is used to confirm the absence of pitting. The devices are subsequently wire-bonded; aluminium pad thinning below 0.2 µm is correlated with lower ball shear strength in assembly.
| Verification point | Test method | Sampling basis | Typical release record |
|---|---|---|---|
| Water content | Karl Fischer titration per ASTM E203-16 | Each incoming container | Vendor certificate of analysis plus ion chromatography trend data |
| pH | ASTM E70-19 | Daily bath sample | Recorded on SPC chart |
| Density at 25 °C | ASTM D4052-22 | Weekly composite | Recorded on SPC chart |
| Kinematic viscosity | ASTM D445-21 | Every 4 hours in fan-out panel line | Alarm at 2× new-bath value |
| Aluminium mass loss | ASTM G1-03 | Qualification lot | ≤0.3 mg/cm² per 30 minutes at 70 °C |
When the dry-film resist has been exposed to a CF4-based descum or has been electroplated in a low-pH copper bath, the top 1–3 µm of the film forms a hardened crust with reduced solvent permeability. Direct immersion into hot EKC-265 without a pre-wet step causes the crust to lift as thin sheets that redeposit on adjacent wafers and create particle defects. A pre-wet step of 60–90 seconds in warm DI water at 35–40 °C hydrates the crust and reduces the burst release of film fragments. In single-wafer spray tools, the same function is achieved by ramping chemical flow from 0.2 L/min to 1.0 L/min over the first 90 seconds. The dry film strip itself uses EKC-265 at 70 °C for 10–15 minutes on 40 µm films; endpoint is determined when reflected light intensity at 550 nm returns to the copper seed-layer baseline. Premature endpoint calls occur if the optical sensor is positioned near the wafer flat or panel edge, where lamination edge bead can be 5–10 µm thicker than the centre. The strip bath is followed by a 30-second hot DI water rinse at 55 °C and an isopropanol vapour dry at 80 °C. Post-strip defect detection uses laser scattering maps; the acceptance limit is 0.02 defects/cm² for an ISO 14644-1:2015 class 1000 cleanroom operation. Terminal products are fan-out packages with copper line widths of 10–20 µm.
For through-silicon via arrays with 10:1 aspect ratio and via depth of 50–100 µm, positive photoresist plugs are used to protect the via bottom during seed-layer etch. After etch, the resist plugs are removed in a two-bath EKC-265 line. The first bath is maintained at 65 °C with low-frequency ultrasonic agitation at 40 kHz to dislodge the hardened plug surface; the second bath is held at 75 °C with 1.0 MHz megasonic energy to remove residues inside the via. The strip time for 60 µm via plugs is 20–30 minutes; if the second bath is skipped, via-bottom residues remain in 20–40% of vias when inspected by cross-section SEM at 5 kV. Post-strip rinse uses sequential DI water at 20 °C and 60 °C to prevent thermal shock cracking of the thin oxide liner; a final vacuum-assisted drying step at 500 Pa removes water from high-aspect-ratio vias. Cleaned TSV wafers then move to barrier deposition and electrochemical copper filling. Organic residue in the via bottom correlates with copper void formation in the subsequent fill step. The final products are interposer wafers for high-bandwidth memory and logic stacking.
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DuPont EKC-265 is supplied as a semi-aqueous electronic/EL-grade positive photoresist stripper and post-etch residue remover for copper redistribution layer, wafer-level bumping, and through-silicon via metallization cleans. The product model designation EKC-265 separates this formulated blend from earlier hydroxylamine-containing and solvent-only chemistries; the EL suffix identifies the grade as subject to reduced trace-metal and particle controls. The full component disclosure is provided in the extended Safety Data Sheet under Regulation (EC) No 1907/2006, Annex II. The product is not a solvent-only stripper and must not be conflated with N-methyl-2-pyrrolidone (NMP)- or dimethyl sulfoxide (DMSO)-based positive resist removers. Physically, the material is an alkaline, water-miscible liquid with a mild amine odour; it is used where exposed copper and aluminum require low-ppb cation control and residue-free water rinsing after thick positive photoresist removal. It is also employed in microelectromechanical systems (MEMS) workflows where the stripper must not leave mobile alkali ions on gold or copper structures.
| Parameter | Typical value | Reference method |
|---|---|---|
| Physical state | Liquid | Visual |
| pH as supplied | 11.0–12.0 | ASTM E70-19 |
| Density at 25 °C | 1.02–1.06 g/cm³ | ASTM D4052-18a |
| Kinematic viscosity at 25 °C | 2–5 mm²/s | ASTM D445-21 |
| Flash point | >93 °C | ASTM D93-20 |
| Water solubility | Complete | Dilution test |
The values in the table are Safety Data Sheet-derived typical ranges for this semi-aqueous amine product class. Lot-specific acceptance criteria appear only on the manufacturer certificate of analysis; they are not overwritten by class-wide literature values.
The Electronic/EL grade is defined by a lot-specific trace-metal and particle matrix rather than by a single published formulation number. Trace-metal quantification is performed by inductively coupled plasma mass spectrometry (ICP-MS) using ASTM D5673-16 or an equivalent method. Control elements include sodium, potassium, iron, copper, aluminum, zinc, and calcium; typical internal limits for an EL-grade stripper of this class are in the low-ppb range, with copper and iron commonly below 20 ppb and sodium below 50 ppb. Because the product is deliberately alkaline and amine-containing, chloride and sulfate are controlled by ion chromatography to prevent metal corrosion after rinse. Liquid particle counts are certified with a laser particle counter calibrated to ISO 21501-4; typical specifications require fewer than 1000 particles/mL at 0.5 µm and fewer than 500 particles/mL at 1.0 µm. The certificate of analysis controls; class-wide literature values cannot substitute for the lot-specific data sheet. In fab qualification, the incoming lot is also screened for total organic carbon and non-volatile residue after forced evaporation at 105 °C for 2 h. The product should be sampled only in an ISO 14644-1 Class 5 environment to avoid airborne contamination during qualification.
Packaging configurations for electronic-grade EKC-265 include 1 L, 5 L, and 20 L high-density polyethylene containers with nitrogen headspace. The material should be stored at 10–25 °C away from direct ultraviolet light; the manufacturer assigns a typical shelf life of 12 months from the date of manufacture when unopened. Storage outside these limits can cause darkening and pH drift; a lot should not be used if the pH deviates beyond the certificate range or if particulate counts exceed the specified limit after submicron filtration is considered.
In 300 mm single-wafer spray tools, EKC-265 is dispensed through heated PTFE/PFA recirculation lines onto the wafer surface at 60–70 °C, with a typical flow rate of 0.5–1.5 L/min per chamber. The process window is narrow: a temperature deviation of more than ±5 °C from the set point shifts the resist dissolution rate and can increase aluminum attack. For immersion baths, batch temperature is maintained at 65 °C ± 3 °C in quartz or PTFE-lined tanks; 316L stainless steel is acceptable only for secondary containment because the amine blend can corrode unpassivated steel and liberate iron. End-point detection is by optical absorbance or by time based on resist thickness; for dry-film resists thicker than 50 µm, a two-step static soak and spin rinse is used. Water content is controlled by refractive index or Karl Fischer titration; accumulated rinse water above 20 vol% reduces strip rate and increases redeposition risk. The bath life in copper bumping lines is commonly limited by dissolved copper loading: published data for this specific configuration is limited, but comparable semi-aqueous amine stripper baths show a drop from 120 h to below 48 h when copper concentration exceeds 10–15 ppm by ICP-MS. Recirculation filters are 0.1 µm PTFE or PFA membrane cartridges installed downstream of the heater to remove particle shedding.
Immersion processing requires stricter control of dissolved oxygen and water content than single-wafer tools. A recirculating bath at low pressure can entrain air, leading to amine oxidation and pH drift; a nitrogen blanket at slight positive pressure of 10–50 Pa is used. Bath pH is monitored by glass electrode; a drop below 10.5 indicates either acid carryover or excessive carbon dioxide absorption. Rinsing after immersion is performed with ultrapure water meeting ASTM D5127-13 Type E-1.2, resistivity 18.2 MΩ·cm at 25 °C and total organic carbon below 5 ppb; no intermediate isopropyl alcohol rinse is required because EKC-265 is water-rinsable, unlike solvent-only resist removers. Metal etch rates on aluminum, copper, and titanium are monitored by sheet resistance or X-ray fluorescence. The absence of fluoride in the formulation reduces titanium attack but also means that post-etch residues with heavy titanium content may require longer exposure than fluoride-based removers. Wafers are not left in the bath beyond process time; extended exposure beyond 60 minutes can cause unwanted undercutting of the aluminum edge and dye penetration under patterned polyimide layers. The batch volume must be sized to the wafer load; a ratio below 2 L of stripper per 200 mm wafer equivalent increases local depletion and produces non-uniform removal across the wafer boat. In production, a recirculating heater with a low-shear magnetically coupled pump is preferred over a centrifugal pump to reduce airborne mist and amine degradation.
EKC-265 is formulated to remove positive photoresist and post-etch residue without aggressively attacking exposed aluminum, copper, titanium, or tungsten. Selectivity is achieved through corrosion inhibitors that form a sacrificial monolayer on exposed metal. On aluminum bond pads, corrosion is assessed by optical microscopy and surface roughness; on copper seed layers, the critical failure mode is galvanic pitting, which occurs when dissolved oxygen is not controlled or when copper concentration in aged baths exceeds 15 ppm. Low-k dielectric compatibility is evaluated by refractive index shift and Fourier transform infrared spectroscopy; methyl depletion in SiOC films increases k-value. EKC-265 is less aggressive to low-k dielectrics than fluoride-containing strippers, but published data for specific low-k materials is limited. The product’s water content avoids the strong capillary stress of pure solvent drying; this is significant in patterned structures with 40 nm half-pitch or smaller features. In copper pillar bumping, a post-strip rinse with dilute organic acid is avoided immediately after EKC-265 unless the acid is buffered, because pH shock can destabilize the inhibitor monolayer and cause copper staining. The neutralization step after EKC-265 is therefore performed with flowing ultrapure water rather than acidified rinse unless the process specification explicitly requires acid rinse.
Compared with N-methyl-2-pyrrolidone (NMP)-based strippers, EKC-265 reduces solvent vapour pressure and eliminates the need for an intermediate organic rinse. NMP is subject to REACH authorisation under Annex XIV; the semi-aqueous profile supports substitution. Compared with dilute aqueous alkaline strippers, EKC-265 has higher solids loading capacity and faster removal of thick positive resists. Compared with fluoride-containing post-etch residue removers, EKC-265 has lower etch rate on Ti/TiN and is therefore preferred in bumping and redistribution layer flows where seed-layer integrity is critical. The following table summarises class-level differences, not lot-specific certificate data.
| Attribute | EKC-265 semi-aqueous amine | NMP-based solvent stripper | Aqueous alkaline stripper | Fluoride-containing residue remover |
|---|---|---|---|---|
| Typical pH | 11.0–12.0 | 7.5–9.5 | 12.0–13.5 | 4.0–7.0 |
| Rinse requirement | Direct DI water | Organic solvent intermediate | Direct DI water | Direct DI water |
| Metal attack | Controlled on Al/Cu/Ti | Low on metals; solvent residue risk | Higher on Al at elevated temperature | Higher Ti/SiO₂ attack |
| Residue removal scope | Positive resist, light post-etch polymer | Positive resist, high-dose implant resist | Positive resist | Post-etch residue, some polymer; not bulk resist |
The comparison is a class-level guide for process engineering evaluation. Actual etch rates and residue-removal performance must be verified on the specific dielectric stack and metallization; published data for this specific configuration is limited.