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Propylene Glycol Methyl Ether Electronic/EL Grade

    • Product Name: Propylene Glycol Methyl Ether 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 735934
    Product Name Propylene Glycol Methyl Ether Electronic/EL Grade
    Chemical Name 1-Methoxy-2-propanol
    Cas Number 107-98-2
    Molecular Formula C4H10O2
    Molecular Weight 90.12 g/mol
    Grade Electronic/EL Grade
    Purity ≥99.9%
    Appearance Clear colorless liquid
    Water Content Very low, electronic grade
    Metal Ion Content Low trace-level metal impurities
    Boiling Point 120.1 °C at 760 mmHg
    Melting Point -96.7 °C
    Flash Point 32.2 °C closed cup
    Specific Gravity 0.922 at 20°C/20°C
    Vapor Pressure 12 mmHg at 25 °C
    Solubility Miscible with water and most organic solvents
    Auto Ignition Temperature 270 °C
    Dielectric Constant Low dielectric constant suitable for electronic applications

    As an accredited Propylene Glycol Methyl Ether 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 200 kg sealed HDPE drums with nitrogen purge, ensuring high-purity EL grade for electronic applications.
    Container Loading (20′ FCL) 20′ FCL loaded with drums/IBCs of electronic-grade propylene glycol methyl ether, secured and labeled for safe transport.
    Shipping Ship as UN 3092, 1-Methoxy-2-propanol, Class 3, PG III. Use clean, sealed drums or IBCs compatible with flammables; keep away from ignition sources. For Electronic/EL grade, prevent contamination and moisture during transport. Mark, label, and document per applicable regulations (road, sea, air).
    Storage Store Propylene Glycol Methyl Ether (Electronic/EL Grade) in tightly sealed, corrosion-resistant containers under dry nitrogen blanketing to preserve high purity. Keep in a cool, dry, well-ventilated area away from oxidizers, heat, open flames, and direct sunlight. Prevent moisture ingress and contamination. Follow first-in, first-out inventory, and maintain recommended storage temperatures to ensure stability and performance.
    Shelf Life Shelf life is typically 2 years when stored in sealed containers under cool, dry, inert conditions.
    Application of Propylene Glycol Methyl Ether Electronic/EL Grade

    Incoming PGME/EL High-Purity Specification Matrix

    ParameterTest MethodTypical Electronic/EL Grade Limit
    Distillation range at 101.3 kPaASTM D1078-15116–126 °C
    Color, Pt-CoASTM D1209-05(2019)≤10
    Density at 20 °CASTM D4052-220.916–0.921 g/cm³
    WaterASTM D1364-02(2012)≤0.05 wt%
    Non-volatile residueASTM D1353-13≤5 mg/100 mL
    Trace metals by ICP-MS after pre-concentrationASTM D5673-16≤10 ppb each; Na/K ≤20 ppb
    Particles ≥0.5 µmSEMI C59-0718≤25 particles/mL

    Which Solvent Parameters Govern Wafer Edge Bead Removal at 300 mm?

    The edge bead removal track uses PGME/EL as the primary medium-boiling component in a solvent blend dispensed through a 0.05 µm PTFE point-of-use filter at 0.5–2.0 mL/s. The wafer is rotated at 800–2200 rpm with exhaust air flow across the coater bowl maintained at 0.3–0.6 m/s. In production EBR blends, PGME/EL is charged at 45–70 wt%, PGMEA at 20–40 wt%, and n-butyl acetate at 5–15 wt%; the ratio is adjusted so that final kinematic viscosity falls between 0.8–1.2 mm²/s at 25 °C and surface tension remains within 26–28 mN/m. These parameters control cut sharpness, backside bevel cleanliness, and re-deposition risk at the wafer edge. The downstream process continues with hotplate soft bake at 90–110 °C, followed by photoresist coating at 1200–4000 rpm and exposure. Terminal finished products are 300 mm silicon wafers with clean edge exclusion zones of 1.0–3.0 mm used in logic, DRAM, NAND, and power-management semiconductor devices. Compliance is defined by SEMI C59-0718 for incoming PGME/EL, water content below 0.05 wt% per ASTM D1364-02(2012), density of 0.916–0.921 g/cm³ per ASTM D4052-22, distillation range per ASTM D1078-15, and trace metal control below 10 ppb by ICP-MS after pre-concentration. A documented processing boundary is that PGME/EL is hygroscopic; if a drum is left open at relative humidity above 60%, water content can exceed 0.1 wt% within 8 h, lowering EBR evaporation rate and leaving a visible resist residue at the wafer edge. Closed stainless steel or fluoropolymer dispensing systems with nitrogen blanketing and point-of-use moisture sensors are used on production tracks to prevent this failure mode.

    Positive-tone DNQ/novolac photoresists formulated with PGME/EL at 5–25 wt% of total mass show a viscosity window of 28–35 cP at 25 °C when measured at 12 rpm on a rotational viscometer per ASTM D2196-20. The formulation process charges solid novolac resin at 15–35 wt%, diazonaphthoquinone photoactive compound at 2–8 wt%, PGMEA at 25–50 wt%, and PGME/EL as the medium-boiling tail solvent to moderate evaporation during spin casting. Mixing is conducted in a 316L stainless steel vessel at 10–25 °C with 0.45 µm pre-filtration and 0.02 µm PTFE membrane final filtration; batch records show viscosity drift of ±0.5–1.0 cP when water content approaches 0.05 wt%, making moisture control central to photospeed repeatability. The downstream process includes spin coating at 1200–4000 rpm, hotplate soft bake at 100–110 °C, i-line exposure at 365 nm, and aqueous-alkaline development. Terminal finished products are i-line and g-line positive photoresists used in 150 mm–300 mm wafer fabs for discrete, analog, and mixed-signal devices. Compliance includes ASTM D4052-22 for density, ASTM D1364-02(2012) for water, and SEMI C59-0718 for electronic-grade solvent cleanliness. A limitation is that PGME/EL cannot replace PGMEA entirely in certain high-solids resists because a boiling-point gap above 8 °C shifts coating uniformity; when the addition exceeds 25 wt%, film thickness standard deviation across a 200 mm wafer rises above 1.5% in coating-track measurements.

    OLED Wet-Strip Bath Composition and Operating Envelope

    In a wet-strip bath for OLED and LCD photoresist rework after dry etch, PGME/EL is maintained at 30–60 wt% and combined with 10–25 wt% alkanolamine, 10–20 wt% sulfolane, 5–15 wt% water, and 0.5–2 wt% corrosion inhibitor. The bath is contained in a PTFE or quartz tank with immersion heating and megasonic agitation at 800–950 kHz. Operating temperature is 40–70 °C, and immersion or spray time ranges from 5–20 min depending on resist thickness of 1.0–3.5 µm. The downstream production sequence includes overflow rinsing with 18 MΩ·cm deionized water, heated nitrogen drying at 60–80 °C, and automated optical inspection for residue. Terminal finished products are OLED display panels, color filter glass, and LTPS TFT backplanes for mobile and large-area displays. Compliance is anchored to RoHS 2011/65/EU Annex II residue limits, REACH Annex XVII restrictions on solvent impurities, and IEC 62321-5:2013 for heavy metal testing after cleaning. Process control uses ASTM D1078-15 for distillation range and ASTM D1209-05(2019) for Pt-Co color. An operational boundary is aluminum compatibility: for aluminum gate structures, the alkanolamine portion must remain at the low end of the range because aluminum etch rate exceeds 0.5 nm/min at 70 °C when amine content rises above 25 wt%. Bath life is typically 72 h before particle counts exceed 50 particles/mL at 0.5 µm, after which point-of-use filtration can no longer maintain defect density.

    When High-Density Interconnects Require Defluxing After 150 µm Pitch Reflow

    PGME/EL is used in semi-aqueous defluxing fluids at 5–15 wt% because its polar and nonpolar solvency removes rosin and no-clean flux residues from under low-standoff components. The downstream production line is an inline spray-in-air cleaner with a pre-wash stage at 35–45 °C, followed by three-stage 18 MΩ·cm deionized water rinsing and forced convection drying at 70–90 °C; spray manifold pressure is held at 5–15 psi. Terminal finished products are HDI PCB assemblies for 5G transceivers, ADAS modules, and implantable medical devices. Cleanliness acceptance is performed by resistivity of solvent extract per IPC-TM-650 2.3.25 with a limit below 1.56 µg NaCl eq/cm², supported by IPC J-STD-001H assembly cleanliness requirements and IEC 61189-5:2006 test methods. The addition ratio is constrained by fire protection engineering: above 15 wt%, the closed-cup flash point of the cleaning bath drops below 32 °C, requiring NFPA 70 hazardous area classification for the spray cabinet when concentration exceeds 10 wt%. A documented failure mode is solder mask swelling at extended contact times above 20 min; production controls therefore limit total chemical contact to 8–12 min. For rework of QFN and BGA pads, manual benchtop cleaning with PGME/EL at high concentration on polypropylene swabs is used only with local exhaust ventilation and contact time below 5 min per site.

    Cathode Slurry Rheology and Co-Solvent Selection Window

    In a documented NMC622 cathode slurry, PGME/EL is added at 2–10 wt% of total slurry mass as a medium-boiling co-solvent with NMP for PVDF binder dissolution. The solvent blend is 70–90 wt% NMP and 10–30 wt% PGME/EL; solids loading is 60–70 wt%, with PVDF at 2–4 wt% and carbon black at 1–3 wt%. Production uses a double planetary mixer under vacuum below 50 mbar and a high-shear rotor-stator disperser at 10–20 m/s tip speed. Final slurry viscosity is controlled to 5,000–12,000 mPa·s at 10 s⁻¹ per DIN 53019-1. The coating line is a slot-die coater running at 0.5–2.5 m/min with drying zones at 80–120 °C and air turnover above 20 air changes/min. Terminal finished products are NMC and LFP electrodes for EV traction cells and stationary energy storage systems. Compliance includes IATF 16949:2016 for automotive battery quality management, REACH Article 33 substance communication, and ASTM D2196-20 for rheological measurement. A critical limit is that residual PGME/EL above 150 ppm in the dried electrode film plasticizes the PVDF binder and reduces peel strength below 0.4 N/cm; drying at 110–120 °C with high air turnover is used to reach 50–100 ppm. Batch-to-batch variation in PGME/EL water content above 0.05 wt% can cause viscosity slump of 800–1200 mPa·s at 10 s⁻¹, so incoming solvent is sampled for water before slurry mixing.

    Post-dicing cleaning of wafer-level chip-scale packages uses PGME/EL at 20–50 wt% in an aqueous or solvent surfactant blend to remove silicon dust, water-soluble die-attach film residue, and trace flux from copper pillar bumps. The cleaning module follows a dicing saw with spindle speed of 30,000–60,000 rpm and spray pressure of 1.5–3.0 bar; substrate temperature is held at 30–50 °C to avoid flash-point excursions. After cleaning, substrates are blow-dried with filtered nitrogen at 50–70 °C and inspected under 50–100× microscopy for residual debris. Terminal finished products are WLCSP, fan-out wafer-level packages, and 2.5D/3D interposers. Compliance uses SEMI C59-0718 for incoming PGME/EL cleanliness, ASTM D1353-13 for non-volatile residue below 5 mg/100 mL, ASTM D4052-22 for density, and ASTM D1364-02(2012) for water. A production boundary exists where PGME/EL concentration above 50 wt% slows die-attach film residue dissolution and can soften epoxy molding compound after 10 min of contact, producing surface haze; the concentration is therefore held below 50 wt% for molded array packages, while bump-only substrates tolerate the upper end of the range for shorter exposure.

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    Certification & Compliance
    More Introduction

    Propylene glycol methyl ether Electronic/EL Grade (PGME, CAS 107-98-2, 1-methoxy-2-propanol, molecular weight 90.12 g/mol) is a high-purity solvent used in semiconductor lithography, flat-panel display cleaning, and advanced packaging. The electronic/EL designation is a grade indicator, not a single product model. Commercial designations encountered include PGME-EL, PGME-UHP, and PGME-S; because these model labels are supplier-specific, the acceptance decision is based on the certificate of analysis and the customer specification rather than the grade suffix. Typical electronic/EL lots are released with an assay of ≥ 99.8%, water ≤ 500 ppm, chloride ≤ 50 ppb, sulfate ≤ 50 ppb, individual metal cations ≤ 10 ppb, and particle counts for particles ≥ 0.5 µm below 50 counts/mL. These values are representative procurement targets compiled from supplier certificate summaries and are not a universal specification; when a SEMI-based specification is invoked, the applicable document is often aligned with SEMI C30 for propylene glycol monomethyl ether. At 101.3 kPa, PGME boils at 120 °C, has a closed-cup flash point of 32 °C, and a viscosity of 1.7 mPa·s at 25 °C. The material is packaged in volumes from 1 L bottles to 200 L drums and stainless steel totes with filtered nitrogen blanketing.

    What separates electronic/EL PGME from standard solvent-grade material?

    Standard solvent-grade PGME is released for paints, coatings, and industrial cleaning, where the main specification is gas-chromatographic assay and water content. Electronic/EL PGME is controlled additionally for nonvolatile residue, extractable anions, trace metal cations, and sub-micrometre particles because the solvent must evaporate without leaving a conductive or corrosive film. In a typical side-by-side comparison, industrial PGME may have chloride in the range of 1 ppm to 10 ppm, while electronic/EL certificates report chloride at ≤ 50 ppb. Sulfate follows a similar reduction. The difference of two to three orders of magnitude is material to aluminium interconnect processing because chloride residue can initiate corrosion under humidity. Alkali metals, iron, copper, chromium, and nickel are controlled at ≤ 10 ppb in electronic/EL lots; these species act as fast-diffusing contaminants or generation-recombination centres if deposited in active device regions. Because no single ISO procedure covers all electronic-grade PGME attributes, customers commonly issue a specification referencing SEMI C30 and add internal methods for anion and metal analysis.

    Representative electronic/EL grade PGME lot-release parameters and industrial PGME reference points
    ParameterElectronic/EL targetIndustrial referenceTypical method
    Assay (1-methoxy-2-propanol)≥ 99.8%≥ 99.0%GC
    Water≤ 500 ppm≤ 1500 ppmASTM E203
    Chloride≤ 50 ppb1 ppm10 ppmIon chromatography
    Sulfate≤ 50 ppb1 ppm10 ppmIon chromatography
    Individual metal cations≤ 10 ppbnot routinely specifiedICP-MS
    Particles ≥ 0.5 µm≤ 50 counts/mLnot routinely specifiedLaser particle counter

    In photoresist formulation, PGME is used to reduce high-viscosity resist polymers into a coatable range between 1.0 mPa·s and 10 mPa·s at 25 °C. Unlike PGMEA, PGME contains a hydroxyl group but no acetate ester, so it does not release acetic acid by hydrolysis in hot water or acidic stripping environments. The solvent boils at 120 °C and has a viscosity of 1.7 mPa·s at 25 °C; these properties reduce early skin formation during spin coating while still allowing the post-apply bake to clear the film. In chemically amplified resist systems, PGME also carries photoacid generators, and low water and amine levels are essential to avoid premature acid neutralization. A resist manufacturer adjusts the PGME/PGMEA ratio to control drying rate, film thickness uniformity, and edge profile. No published universal correlation between PGME fraction and line-width roughness is available; each resist formulation requires a spin-speed curve and thermal stability study on the target coater track.

    Water and amine control in chemically amplified resist processing

    Water and amine control in electronic/EL PGME is tied to the reaction-diffusion chemistry of chemically amplified resists. During a post-exposure bake at temperatures between 90 °C and 120 °C, photoacid generators release a catalytic acid; water participates in the deprotection reaction, while trace amines neutralize acid and create footing or T-top profiles. If the solvent used for resist dilution or edge cleaning contains water above 0.1% or amine contamination at parts-per-billion levels, the acid concentration at the resist bottom may drop, producing radial CD nonuniformity at the wafer edge. The effect is amplified at smaller linewidths because the relative contribution of trace contaminants is larger. Published kinetic data are resist-system-specific; resist suppliers provide maximum allowable solvent water and amine concentrations for each formulation. In production, a lot of PGME with water at 450 ppm may be acceptable for edge-bead removal but rejected for resist dilution, depending on the resist vendor’s process window.

    If PGME is dispensed as an edge-bead remover on a 300 mm coater track

    On a production coater track, electronic/EL PGME is supplied to the edge-bead removal nozzle from a pressurized canister fitted with a point-of-use filter of 0.05 µm or 0.1 µm retention. The nozzle directs the solvent at the wafer edge while the wafer rotates at 800 rpm to 1500 rpm; typical edge-bead removal flow rates range from 1 mL/min to 20 mL/min, depending on resist thickness and edge exclusion. Because PGME has a vapor pressure of approximately 1.2 kPa at 20 °C, track exhaust must maintain a stable downflow to prevent solvent droplets from re-condensing on the wafer backside. When the water content exceeds 0.1%, the drying front at the edge may shift and leave an organic residue at the boundary; the defect appears as a radial CD deviation or ring-shaped mark on the wafer map. Lot changeover on the track is qualified by total organic carbon and particle counts in the drain line, not by fixed flush time alone.

    Metal cation limits in electronic/EL PGME are process-critical because the solvent may be the last liquid to contact a patterned wafer before etch, metallization, or dielectric deposition. Sodium and potassium are mobile in silicon oxide and can shift threshold voltage; iron and copper introduce midgap states; chloride and sulfate form aggressive residues during plasma or thermal processing. In high-aspect-ratio structures with aspect ratios above 20:1, capillary retention concentrates nonvolatile impurities at the bottom meniscus, so a particle limit of ≤ 50 counts/mL for particles ≥ 0.5 µm is coupled with a cation limit of ≤ 10 ppb per element. Some cleanroom processes impose a lower total particle budget and require filtration through 0.02 µm membranes immediately before the dispense nozzle. Published defect-level data for specific device nodes are limited because acceptance thresholds are generally proprietary; however, incoming-solvent release gates based on cation and particle limits are standard practice in wet-bench and track operations.

    Replacing isopropanol in a wet-bench cleaning sequence

    PGME differs from isopropanol in solvency and evaporation rate. Isopropanol has a boiling point of 82.5 °C and a viscosity of 2.0 mPa·s at 25 °C; PGME boils at 120 °C and has a viscosity of 1.7 mPa·s at 25 °C. PGME is a stronger solvent for novolak and polyhydroxystyrene residues, but its slower evaporation requires a defined rinse sequence. The recommended sequence is PGME contact followed by ultrapure water or isopropanol rinsing and heated nitrogen drying. PGME is fully miscible with water, unlike n-butyl acetate, so rinsing is simplified and flash corrosion is reduced. Because the molecule does not contain an ester group, it will not hydrolyse to acetic acid in acidic or high-temperature cleaning baths; this is an advantage over PGMEA when corrosion-sensitive aluminium or copper/low-k structures are present. Published compatibility data for specific low-k dielectrics remain limited, and screening on patterned test wafers is required before conversion from an existing solvent.

    Electronic/EL PGME is hygroscopic and must be stored under dry nitrogen at relative humidity < 60%. High-density polyethylene or fluoropolymer-lined containers are commonly used; passivated stainless steel is acceptable only when the product is not held for extended periods near the water specification limit. Drums and totes are blanketed with 0.05 µm filtered nitrogen after each withdrawal to limit moisture uptake. If moisture ingress exceeds 500 ppm, the material is either dried through molecular sieve or membrane systems or rejected for lithographic use. The solvent should not be stored or transported with amine-based cleanroom chemicals because trace ammonia and amines can partition into the headspace and later poison chemically amplified resists by neutralizing photoacid. Wetted parts should be PTFE, high-density polyethylene, or stainless steel; elastomeric seals must be perfluoroelastomer rather than EPDM to avoid extractable contamination.

    The substitution of PGMEA by PGME changes spin-speed curve and hydrolysis behavior

    PGME and PGMEA are both propylene glycol ether solvents used in semiconductor fabrication, but PGME is an alcohol ether and PGMEA is its acetate ester. PGMEA has a boiling point of 146 °C, a flash point of 45 °C, and a viscosity of 1.2 mPa·s at 25 °C; PGME has a boiling point of 120 °C, a flash point of 32 °C, and a viscosity of 1.7 mPa·s at 25 °C. PGME dries faster and is more hydrophilic, while PGMEA has stronger solvency for certain acrylate and cyclic olefin resists and leaves a higher-boiling residual film. When PGME replaces PGMEA, the spin-speed curve shifts toward lower spin speeds because the lower viscosity and faster evaporation reduce wet film thickness. The absence of the acetate group in PGME makes it less prone to generating acetic acid under hot water or acidic stripping conditions, which is beneficial for aluminium and copper/low-k compatibility. Comparative compatibility data for specific low-k dielectrics are limited; a solvent substitution should be validated on patterned test wafers with post-etch electrical and reliability checks.

    Analytical lot release for electronic/EL PGME begins with gas chromatography for assay and isomer distribution. The primary isomer is 1-methoxy-2-propanol; 2-methoxy-1-propanol is typically limited to ≤ 0.3%. Water is measured by ASTM E203 volumetric Karl Fischer titration. Anions are quantified by ion chromatography, and trace metals by inductively coupled plasma mass spectrometry. Liquid particle counts are performed with a particle counter calibrated to ISO 21501-2. During filling, the solvent is passed through a 0.05 µm membrane filter, and the container is sealed under filtered nitrogen. A release sample is drawn from the closed container after filling because sample handling can introduce particles; the reported particle value therefore reflects the packaged lot rather than the bulk feed. These measurements are repeated at point-of-use only when the solvent is used in critical lithography layers or when a contamination event is suspected on the track.

    Flat-panel display manufacturing uses electronic/EL PGME as a cleaning solvent for organic residues after photoresist stripping and as an edge-bead remover on large glass substrates. In a display wet-bench with substrate sizes of 2.2 m × 2.5 m and larger, the solvent is dispensed through multi-nozzle heads and removed by vacuum exhaust. The same particle and cation limits are applied, but the larger substrate area magnifies the visual defect density produced by residue, so a particle budget below 50 counts/mL for particles ≥ 0.5 µm is a standard incoming control. Megasonic cleaning baths operating at 40 kHz or 1 MHz may use PGME in a pre-rinse step, provided the bath is vented and the vapor concentration is maintained below the applicable flammable limit. The grade is also used in advanced packaging for flux residue removal and underfill preparation, where low extractable ions reduce electrochemical migration risk on fine-pitch copper pillars.

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