| HS Code | 572553 |
| Appearance | White fine powder |
| Chemical Composition | Polyvinyl butyral (PVB) resin |
| Butyral Content | 64 - 68 % |
| Hydroxyl Content | 29 - 33 % |
| Residual Acetyl Content | 0.5 - 3 % |
| Specific Gravity | 1.08 - 1.11 |
| Glass Transition Temperature | 65 - 72 °C |
| Solution Viscosity | 30 - 60 mPa·s (5 wt% in ethanol at 20 °C) |
| Refractive Index | 1.488 - 1.492 |
| Water Absorption | 0.4 % (24 h) |
| Melting Point Softening Range | 190 - 210 °C |
| Solubility | Soluble in alcohols, ketones, esters, and chlorinated solvents; insoluble in water |
As an accredited S-LEC BM-2 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | S-LEC BM-2 is supplied in 25 kg sealed polyethylene-lined paper bags, ensuring moisture protection and safe handling. |
| Container Loading (20′ FCL) | S-LEC BM-2 shipped in 20′ FCL, packed in moisture-proof bags on pallets, securely stowed for safe transport. |
| Shipping | S-LEC BM-2 is a polyvinyl butyral resin powder. It ships as a non-hazardous chemical in sealed bags or drums to prevent moisture pickup and contamination. Avoid creating airborne dust during handling and keep away from ignition sources. Not regulated as dangerous goods for road, sea, or air transport. |
| Storage | Store S-LEC BM-2 in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep the original container tightly closed to prevent moisture absorption and contamination. Avoid exposure to high humidity. Use clean, dry tools when handling. Under proper storage conditions, the material remains stable for its intended shelf life. |
| Shelf Life | S-LEC BM-2 has a typical shelf life of 12 months when stored unopened in a cool, dry place. |
In solvent-based flexographic and gravure lamination printing for surface-print snack packaging, S-LEC BM-2 functions as the PVB film former in alcohol-soluble ink systems. The resin is pre-dissolved at 10–15 wt% in a solvent blend of ethanol, ethyl acetate and propyl acetate under a Cowles high-shear dissolver at 40–50 °C. Complete chip inversion is confirmed when a Hegman gauge reading drops below 5. Pigment concentrates are then milled on a horizontal bead mill charged with 0.6–0.8 mm yttria-stabilized zirconia beads; base inks are adjusted to a press viscosity of 18–25 s Zahn Cup #2 at 25 °C. On corona-discharge-treated biaxially oriented polypropylene and polyethylene film, surface energy is maintained at 38–42 mN/m. Tape adhesion is checked according to ASTM D3359 Method B after 24 h of conditioning at 23 °C and 50 % relative humidity. A target classification of 4B or 5B is expected for non-UV inks; lower values indicate insufficient corona or excessive slip-agent bloom. In laminate structures, the dried ink layer must not exceed 5 mg/m² residual solvent when measured by headspace gas chromatography because higher volatile residues lower heat-seal strength and can generate off-odours. Laminating bond strength is evaluated per ASTM F904 on the printed web under standard T-peel conditions. BM-2 is suitable where ambient-temperature adhesion to metallised PET and solvent release in high-speed CI flexo presses between 250 and 350 m/min are required. The resin is not recommended for retort, boil-in-bag or high-acid filling because PVB absorbs moisture and loses interfacial adhesion under hydrothermal stress.
On solvent-cleaned hot-rolled steel and blast-cleaned aluminium, a wash primer built on BM-2 is applied as a thin conversion-primer layer. A typical starting formulation contains 7–9 wt% BM-2 resin solids, 3–5 wt% phosphoric acid 85 %, 5–8 wt% zinc phosphate, and a co-solvent balance of isopropanol, n-butanol and toluene-free diluent. The acid component etches the metal oxide layer and activates adhesion, but the same reactivity imposes a dry-film ceiling. Spray application through HVLP equipment at 0.8–1.2 bar atomising pressure is controlled to a wet-film thickness of 15–25 µm, yielding 5–8 µm dry. Above 8–10 µm dry film, phosphoric acid residues can remain at the interface and interfere with epoxy or polyurethane crosslinking. The primer must be overcoated within 16–24 h at 20–25 °C and below 60 % relative humidity; longer delays can close the surface and reduce intercoat adhesion. In closed stainless-steel pressure pots, pot life is 8–12 h. Amine-functional additives, ketimine curing agents and strong alkaline cleaners are incompatible because they neutralise the acid and destabilise the PVB solution. For corrosion testing, scribed panels are exposed to neutral salt spray per ISO 9227 for 240–500 h and evaluated for blistering and creep according to ISO 4628-2 and ISO 4628-8. Pull-off adhesion after overcoating is measured to ISO 4624, with acceptance typically not less than 5 MPa on an epoxy topcoat system. The use of chromate pigments is governed by REACH Annex XVII restrictions; zinc phosphate is the standard non-toxic alternative but gives slower early corrosion performance.
For tape casting of barium titanate dielectric layers in multilayer ceramic capacitors, BM-2 is dissolved at 12–15 wt% in a 60:40 toluene-to-ethanol azeotrope before addition of ceramic powder. A 55–60 vol% solids slurry is prepared in a planetary mixer under vacuum to remove trapped air; a phosphate ester dispersant is added at 0.5–1.2 wt% of ceramic solids and a benzyl butyl phthalate or dibutyl phthalate plasticizer at 4–6 wt% of PVB solids. The final slurry viscosity is held between 1500 and 4000 mPa·s at a shear rate of 10 s⁻¹ on a cone-plate rheometer. In a continuous tape-casting line, the slurry is fed through a doctor blade with a gap of 50–250 µm onto a silicone-coated PET carrier moving at 0.3–1.0 m/min. Drying takes place in three zones at 50–90 °C with counter-current air to avoid surface skinning. Green tape thickness typically ranges from 25 to 150 µm. The binder imparts green strength and prevents cracking during blanking, stacking and lamination. Green density after drying is typically 55–60 % of theoretical, measured by immersion per ISO 18754. Debinding is the critical rate-limiting unit operation: heating is ramped at 0.2–0.4 °C/min to 450 °C, held for 60 min, then ramped at 1 °C/min to 650–700 °C. Airflow must be sufficient to oxidise PVB decomposition products. Residual carbon after burnout is kept below 0.05 wt% for capacitor reliability. Published data for BM-2 carbon residue after air debinding under a specific furnace profile are limited; thermogravimetric analysis indicates the main PVB decomposition interval between 350 and 420 °C. The entire casting and drying section must be rated for explosion-proof operation because toluene/ethanol mixtures are used.
| Application | Critical processing variable | Acceptable window | Primary test method |
|---|---|---|---|
| Flexographic lamination ink | Press viscosity / substrate surface energy | 18–25 s Zahn Cup #2 at 25 °C; 38–42 mN/m | ASTM D3359 Method B |
| Wash primer | Dry-film thickness / overcoating interval | 5–8 µm; 16–24 h | ISO 9227 / ISO 4624 |
| Ceramic tape casting | Debinding ramp rate / residual carbon | 0.2–0.4 °C/min to 450 °C; <0.05 wt% | ISO 18754 |
| PVB interlayer extrusion | Melt pressure / melt temperature | 80–140 bar; 190–210 °C | ISO 12543-2 |
| Heat-seal primer | Dry coating weight / seal dwell | 0.8–2.5 g/m²; 0.5 s | ASTM F88 |
BM-2 is compounded with plasticizer to produce PVB interlayer sheet for laminated safety glazing. The resin is pre-dried to a moisture content below 0.2 % at 50–60 °C in a desiccant dryer for 4–6 h. The formulation combines BM-2 with 22–32 phr triethylene glycol di-2-ethylhexanoate, 0.1–0.3 phr hindered phenolic antioxidant and, in some systems, 0.5–1.0 phr UV stabilizer. Mixing is carried out in a co-rotating twin-screw extruder with an L/D ratio of 40:1, barrel temperatures of 190–210 °C and screw speed of 250–350 min⁻¹. Melt pressure before the screen pack is maintained between 80 and 140 bar. Pressure excursions above 160 bar or amperage fluctuations beyond ±5 % indicate poor plasticizer absorption, moisture-backed steam generation or partially melted resin. The melt is calendered through polished chromed rolls at 60–80 °C to produce sheet of 0.38 mm or 0.76 mm gauge. Interlayer sheet must satisfy optical and mechanical requirements under ISO 12543-2, while finished laminated glass is classified according to EN ISO 12543-1 and tested under ANSI Z97.1 for glazing used in safety applications. Adhesion to glass is determined by the pummel test after autoclave lamination at 140 °C and 1.2 MPa for 60–90 min; acceptable pummel values typically fall between 4 and 8 units, although published data for BM-2-specific pummel values are limited. Because BM-2 is an intermediate-viscosity PVB grade, sheet tensile and tear performance are lower than those made from high-molecular-weight grades; therefore it is positioned for standard architectural and automotive side-laminated parts rather than high-load structural or hurricane-glazed assemblies.
For heat-seal priming of aluminium foil lidding in pharmaceutical blister packaging, BM-2 is applied as a styrene-free alcohol-soluble primer from ethanol or ethyl acetate solution. The solution is metered by a ceramic anilox roll at 60–80 lines/cm onto 20–25 µm foil. Wet application is dried in forced-air ovens at 70–100 °C to a dry coating weight of 0.8–2.5 g/m². A small addition of dioctyl adipate, 2–5 phr on resin solids, reduces film brittleness and improves seal initiation. Sealing is performed against PVC or PVdC blisters at 130–160 °C, 0.3 MPa jaw pressure and 0.5 s dwell. Peel strength is measured according to ASTM F88, with minimum values for pharmaceutical lidding generally above 4 N/15 mm. Hot-tack is assessed immediately after seal jaw opening to prevent blister peel-back. Because PVB absorbs atmospheric moisture, storage of coated foil at relative humidity above 60 % can lower seal consistency; sealed edge integrity should be retested after 24 h at 23 °C and 50 % relative humidity. BM-2 has low odour and is free of aromatic isocyanates, but it is not used for retortable lidding structures where prolonged steam exposure plasticises the primer and causes progressive peel-strength loss.
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S-LEC BM-2 is a polyvinyl butyral resin supplied as a free-flowing white powder and assigned to the medium solution-viscosity tier of the S-LEC B series. The resin is a terpolymer composed primarily of vinyl butyral, residual vinyl alcohol, and a low vinyl acetate fraction. This distribution of functional groups controls dissolution in ethanol/toluene and ethyl acetate/ethanol blends, governs hydrogen-bonding adhesion to glass, aluminium oxide, and corona-treated polymer films, and influences tensile elongation after solvent evaporation. In the S-LEC B range, BM-2 is positioned between low-viscosity BL grades and high-viscosity BH grades; the grade is selected where a formulation requires increased film cohesion relative to BL resins but still needs filtration and coating behaviour that a high-molecular-weight BH resin cannot provide. Primary end uses include ceramic green-sheet binders for multilayer ceramic capacitors, solventborne printing ink binders, and solventborne adhesion primers for metal oxides.
The certificate of analysis for each lot of S-LEC BM-2 reports hydroxyl group content, acetate content, butyral content, volatile matter, ash residue, and solvent viscosity. These values are not fixed constants because industrial acetalization of polyvinyl alcohol with butyraldehyde is controlled by reaction time, catalyst removal, and washing; therefore, lot-to-lot variability exists in any PVB resin. Table 1 summarises the manufacturer-published typical range for BM-2. Incoming inspection on a production line usually repeats Brookfield solution viscosity and volatiles because solvent viscosity shifts coating thickness and drying load, whereas full compositional analysis is reserved for supplier qualification and root-cause investigations. The table values should be read as reference ranges; the lot-specific values on the current certificate of analysis take precedence for process adjustments.
| Property | Typical range | Test method / condition |
|---|---|---|
| Brookfield solution viscosity | 4.0–9.0 mPa·s | ASTM D2196 / ISO 2555, 10 mass% in 95:5 ethanol:toluene at 20 °C |
| Density | 1.10–1.12 g/cm³ | ISO 1183-1 |
| Volatile matter | ≤2.0 mass% | ISO 3251, 105 °C, 3 h |
| Ash residue | ≤0.05 mass% | ISO 3451-1, 600 °C, 2 h |
| Hydroxyl content | 20.0–23.0 mass% | JIS K6728 |
| Vinyl acetate content | ≤3.0 mass% | JIS K6728 |
| Glass transition temperature | 68–72 °C | ISO 11357-2, DSC, 10 °C/min, second heating |
| Tensile strength of cast film | 18–24 MPa | ISO 527-2, 23 °C |
| Elongation at break | 15–40% | ISO 527-2, 23 °C |
The hydroxyl content is analytically expressed on a mass basis by the supplier; users should not convert directly to molar hydroxyl fraction without applying the molecular-weight basis of the vinyl alcohol repeat unit because the resin is a terpolymer. The residual acetate fraction is kept low to reduce plasticization and low-temperature water uptake, while the butyral fraction supplies the hydrophobic spacing between hydrogen-bonding sites that gives the resin its balance of ethanol solubility and film strength.
In MLCC green-tape processing, S-LEC BM-2 functions as the primary polymeric binder in a high-solids dispersion of barium titanate. A representative production slurry contains 65–75 mass% BaTiO₃, 25–35 mass% solvent, 0.5–1.5 mass% phosphate ester dispersant, 3.0–5.0 mass% S-LEC BM-2, and 0.5–1.5 mass% plasticizer such as dibutyl phthalate or benzyl butyl phthalate. The powder is pre-dried to remove surface moisture before addition because water competes with the dispersant and raises slurry yield stress. Dispersion is carried out in a high-shear dissolver or bead mill; the tip speed of the dissolver is held at 15–20 m/s for 30–60 min, and the slurry temperature is maintained below 35 °C to prevent solvent evaporation. After dispersion, the slurry is filtered through a 10 µm absolute-rated membrane to remove agglomerates and undispersed resin particles.
The filtered slurry is cast onto polyethylene terephthalate carrier film with a doctor blade gap of 100–250 µm. Drying in a three-zone oven at 70–100 °C reduces residual solvent to 0.2–1.5 mass%. The dried green tape is wound at line tension below 100 N/m to avoid blocking. Green tensile strength measured on 25 µm-thick tape by ASTM D882 is typically 1.5–3.0 MPa when binder loading is 3.0–5.0 mass%; below this range, punching and stacking operations generate edge cracking; above it, the binder leaves carbonaceous residue during co-firing. The burnout window is established by thermogravimetric analysis per ASTM E1131 in air at 10 °C/min; decomposition begins near 220 °C and multi-step oxidation is complete by 550 °C. The low ash value in Table 1 is a gate criterion because alkali residues in barium titanate layers shift capacitance-temperature behaviour and reduce insulation resistance.
On full-width tape-casting lines above 1.0 m, lot-to-lot Brookfield viscosity variation of ±1.0 mPa·s in the incoming BM-2 has been observed to move wet film thickness by 3–5% under constant doctor blade pressure. Inline solvent addition using a rotational viscometer operating at 20 Hz with feedback to the mix tank is used to hold coat weight within ±2%. When a slot-die coater is used instead of a doctor blade, the target apparent viscosity is typically 200–800 mPa·s at 10 s⁻¹; published data for S-LEC BM-2-specific slurry rheology at these shear rates is limited, so pilot-scale rheology scans are required for each new lot and powder supplier.
For solventborne flexographic and gravure inks, S-LEC BM-2 is dissolved at 10–20 mass% in ethanol/ethyl acetate or ethanol/n-propyl acetate using a high-torque dissolver. Dissolution temperature is held at 40–50 °C because higher temperatures accelerate solvent loss without eliminating microgels. At a printing viscosity of 20–25 s measured by ISO 2431 with a 4 mm cup at 25 °C, a BM-2-containing gravure ink transfers with acceptable cell emptying from 60–80 lines/cm engravings, but the higher solution viscosity relative to low-viscosity PVB can require 0.2–0.5 mass% of a silicone-free flow agent to maintain leveling on corona-treated polyester. Adhesion results are influenced by the hydroxyl fraction; the same hydrogen-bonding hydroxyl groups that bond to glass and aluminium oxide also interact with oxidised polymer surfaces.
The residual hydroxyl group content of S-LEC BM-2 is the main compositional variable controlling room-temperature solubility in anhydrous ethanol and adhesion to silanol-bearing surfaces. When the hydroxyl content rises above approximately 25 mass%, interchain hydrogen bonding reduces cold solvent solubility and can produce a yield stress at high solids. When the hydroxyl content falls below approximately 17 mass%, ethanol dissolution improves but adhesion to glass and aluminium oxide declines because fewer proton-donating hydroxyl groups are available for hydrogen bonding. The 20.0–23.0 mass% range in Table 1 places S-LEC BM-2 inside the adhesion/solubility window required for ceramic binders and polar film primers. On aminosilane-primed soda-lime glass, a cast film of BM-2 from a 10 mass% solution dried at 60 °C can exceed 2.0 N/mm T-peel adhesion when measured by ISO 8510-2; this value is substrate-limited and should be re-verified after any change in glass washing, silane concentration, or cure temperature. The butyral groups provide hydrophobic spacing that limits water sensitivity; the acetate groups are kept low to avoid plasticization and moisture gain at elevated relative humidity.
Substitution of S-LEC BM-2 for a low-viscosity PVB such as S-LEC BL-1 at equal resin solids raises ink viscosity and dry film tensile strength but lowers re-solubility and increases minimum drying-web temperature. In a representative flexographic ink pigmented with carbon black at 15 mass% on 12 µm corona-treated polyester, print trials showed tape adhesion per ASTM D3359 improve from 4B to 5B when BM-2 replaced BL-1, while static coefficient of friction increased from 0.25 to 0.32. The higher glass transition temperature of BM-2 requires the hot-air web temperature to be raised by 5–8 °C to achieve residual solvent below 5 mg/m²; otherwise blocking occurs at the rewind. Comparative typical values are listed in Table 2.
| Property | S-LEC BL-1 | S-LEC BM-2 | S-LEC BH-3 | Test method |
|---|---|---|---|---|
| Brookfield solution viscosity | <2.0 mPa·s | 4.0–9.0 mPa·s | >20 mPa·s | ASTM D2196, 10 mass% in 95:5 ethanol:toluene at 20 °C |
| Glass transition temperature | 63–66 °C | 68–72 °C | 73–76 °C | ISO 11357-2 |
| Tensile strength | 14–18 MPa | 18–24 MPa | 22–28 MPa | ISO 527-2 |
| Elongation at break | 30–60% | 15–40% | 10–25% | ISO 527-2 |
| Ash residue | ≤0.05 mass% | ≤0.05 mass% | ≤0.05 mass% | ISO 3451-1 |
The viscosity increase when moving from BL-1 to BM-2 is the primary formulation difference. Ink makers compensate by reducing total resin solids by 1–3 mass% and increasing slow solvent by 5–10% of the solvent mass to maintain open time. If the formulation is not adjusted, gravure cells fail to empty at press speeds above 200 m/min, and foaming becomes more persistent in the ink pan. The higher molecular weight of BM-2 improves pigment binding and rub resistance but also makes dried ink films less readily re-dissolvable on press parts; cleaning cycles with a solvent blend containing 20–30% methoxypropyl acetate may be required.
Under Regulation (EC) No 1272/2008, S-LEC BM-2 is not classified as a hazardous substance in the supplied solid form. Dust from bag handling is controlled as organic nuisance dust; an occupational exposure limit of 3 mg/m³ total particulate is typically applied according to the ACGIH PNOS fraction, but local regulation must be checked. Registration under REACH Regulation (EC) No 1907/2006 is maintained by the manufacturer for industrial use. Food-contact status is not automatic; users must verify compliance with 21 CFR 175.105 or 21 CFR 177.1670 for the intended article because migration and extractive limits depend on the final packaging structure and coating thickness. S-LEC BM-2 should be stored in sealed polyethylene-lined bags at 10–30 °C and relative humidity below 60%; at relative humidity above 60%, pre-drying at 50–60 °C for 2–4 h is required before dissolution. High-acid-number additives with acid values above 5 mg KOH/g should be avoided because acid-catalyzed hydrolysis of the acetal groups degrades molecular weight and causes solution viscosity to drift downward over storage.