| HS Code | 620445 |
| Appearance | White fine powder |
| Specific Gravity | 1.08–1.10 |
| Refractive Index | 1.485–1.490 |
| Glass Transition Temperature | 65–70 °C |
| Average Molecular Weight | 100,000–150,000 |
| Viscosity 5 Ethanol Solution 20 C | 30–50 mPa·s |
| Hydroxyl Group Content | 28–32 wt% |
| Butyral Group Content | 63–68 wt% |
| Acetyl Group Content | 1–3 wt% |
| Tensile Strength | 30–35 MPa |
As an accredited S-LEC BX-5 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | S-LEC BX-5 is supplied in 20 kg moisture-resistant multi-layer paper bags with a polyethylene inner liner. |
| Container Loading (20′ FCL) | Load S-LEC BX-5 into a 20-foot FCL, secure pallets, protect from moisture, and follow chemical handling guidelines. |
| Shipping | Ship S-LEC BX-5 as a non-hazardous resin in sealed multi-layer bags or drums to prevent moisture absorption. Keep in dry, ventilated containers away from heat and ignition sources. Avoid prolonged exposure to humidity and direct sunlight. No special hazmat labeling required under normal conditions, but secure loads to prevent damage during transit. |
| Storage | Store S-LEC BX-5 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep the original container tightly sealed to prevent moisture absorption and contamination. Maintain moderate temperatures, avoid high humidity, and follow shelf-life guidelines. Ensure area is clean and incompatible materials are stored separately. |
| Shelf Life | Shelf life of S-LEC BX-5 is typically two years when stored in original sealed container away from heat, moisture, and sunlight. |
In multilayer ceramic capacitor production, S-LEC BX-5 is introduced as the high-molecular-weight polyvinyl butyral binder phase for X7R and X5R barium titanate dielectric tape casting. The slurry is compounded on a high-shear dissolver until a Hegman gauge reading below 5 µm is reached, then passed through a three-roll mill with chilled rolls to reduce agglomerates without exceeding a stock temperature of 35 °C. A typical solvent blend is a 60:40 toluene-to-ethanol mixture, with total solids held between 50 wt% and 70 wt%. Binder concentration is maintained at 6–12 wt% of the ceramic powder; butyl benzyl phthalate or dioctyl phthalate plasticizer is added at 25–40 phr of binder to lower glass transition temperature and prevent edge cracking during slitting. Slurry rheology is controlled to 800–2,000 mPa·s at 25 °C using a Brookfield RVT viscometer with spindle 5 at 20 rpm, and the slurry is vacuum de-aired below 50 mbar before casting. Tape is deposited through a doctor blade with a gap of 10–150 µm onto silicon-coated PET carrier at 0.5–5 m/min. Solvent evaporation in a multi-zone dryer at 70–90 °C produces a green sheet with residual solvent below 2 wt% as measured by thermogravimetric analysis. Green tensile elongation is measured according to ASTM D882; a value of at least 5% is generally required for downstream punching and lamination without microcracking. On production tape-casting lines, surface tension is maintained between 28–32 mN/m to avoid cratering on the carrier film. Batch-to-batch variation in PVB hydroxyl content can alter green tack; if the hydroxyl value shifts by more than 1 mol%, the plasticizer ratio is adjusted to keep the plasticized binder glass transition temperature within the range specified on the supplier lot certificate. Green sheet storage above 60% relative humidity can cause moisture uptake and registration drift; unprocessed reel stock is therefore held at 23±2 °C and 30±5% RH until cutting. Binder burnout is performed in air at 350–450 °C with a ramp rate of 1–2 K/min through the primary decomposition region, and the resulting ceramic layer is sintered to a fired thickness below 2 µm for high-capacitance MLCC. Compliance qualification for the finished capacitor follows IEC 60384-22 for Class 2 temperature-stable devices, and RoHS 2011/65/EU applies to terminations containing lead-free solder coatings. Published data for this specific BX-5 casting configuration is limited; batch hydroxyl content and molecular weight distribution should be verified against the supplier certificate of analysis to maintain constant green density and lamination tack.
S-LEC BX-5 enters Ag/Pd thick-film paste formulations primarily as a carrier resin that must combine high solution viscosity at low solids with clean oxidative decomposition during firing. A representative precious-metal paste contains 75–85 wt% Ag or Ag/Pd flake, 10–20 wt% binder solution, 1–5 wt% low-softening lead-free glass frit, and 0.5–2 wt% amphiphilic dispersant. The BX-5 solution is prepared in a high-boiling solvent blend such as terpineol and butyl carbitol acetate, then predispersed with a high-speed mixer and homogenized on a three-roll mill with roll gaps below 20 µm. Paste viscosity is measured on a Brookfield HBT viscometer at 10 rpm and adjusted to 100,000–300,000 mPa·s; this range maintains screen-printing shear thinning while preventing slump after deposition through a 325-mesh stainless-steel screen with an emulsion thickness of 10–20 µm. During burnout, the PVB is decomposed in air at 350–450 °C, and the residual ash is quantified according to ISO 3451-1. A high-polymerization grade such as BX-5 contributes longer chain entanglement, which can reduce paste settlement during an 8-hour production shift; solvent evaporation-induced viscosity drift is typically held below 10% by controlling the mill cover temperature below 20 °C. Production failure modes include dried PVB agglomerates transferring from the mill cover to the screen mesh, so end-of-shift paste is recovered and stored in sealed containers under a slow solvent headspace to limit viscosity rise above 15% of the original value. The terminal application is the internal electrode layer of Ag/Pd MLCCs, as well as hybrid microcircuit conductors where fired line widths below 200 µm are printed and then fired in belt furnaces. The binder is not suitable for base-metal Ni or Cu systems fired in reducing atmospheres because incomplete combustion products can leave carbon residues; for those systems a different binder chemistry is required. Compliance for printed circuit assemblies is assessed under IEC 61249-2 and RoHS 2011/65/EU for hazardous substances in the finished laminate or component.
Where solvent-based flexographic or gravure inks are formulated for reverse-printed BOPP and PET lamination structures, S-LEC BX-5 functions as a high-molecular-weight vinyl butyral binder that provides wetting on corona-treated substrates and free hydroxyl groups for subsequent crosslinking with aliphatic polyisocyanate. A starting ink formulation contains 5–10 wt% BX-5 binder, 15–30 wt% pigment dispersion, 50–70 wt% ethanol/ethyl acetate solvent blend, and 1–3 wt% slip or adhesion additives. The BX-5 is dissolved under high-speed agitation at 40–50 °C until the solution is clear and filtered through a 10 µm absolute filter. Press viscosity is measured by ISO 2431 using a DIN 4 mm flow cup at 25 °C and adjusted to 18–25 s; for gravure cylinder engraving depths of 30–45 µm, higher binder molecular weight may require a slight increase in ethyl acetate to maintain a Brookfield viscosity below 150 mPa·s at 100 rpm. Adhesion is assessed after lamination with ISO 2409 cross-cut testing; a class 0 or 1 rating is required on BOPP with a minimum surface energy of 38 mN/m. Peel strength of the laminated structure is measured according to ASTM F88 with heat-seal jaws at 120 °C and 0.3 MPa for 1 s; the binder contribution is accepted when the seal remains non-delaminated at the ink/adhesive interface. Pot life after addition of a polyisocyanate crosslinker at an NCO:OH molar ratio of 1.2:1 is typically limited to 4–8 h at 25 °C, and viscosity rise beyond 20% of initial reading indicates incipient gelation. The terminal products are snack food laminates, overwrap films, and pharmaceutical sachet structures where PVB is permitted as a component of an FDA 21 CFR 175.105-compliant adhesive system only after migration testing is completed for the specific food contact condition. No single-vendor dataset covers all ethanol/ethyl acetate ratios; BX-5 solution viscosity is measured against the supplier lot certificate before the pigment loading is fixed.
A chromium-free wash primer compounded with S-LEC BX-5 is prepared as a single-pack etch primer in which the polyvinyl butyral binder is acid-modified to bond to metal oxides. The liquid base contains 8–12 wt% BX-5, 2–4 wt% of 85% phosphoric acid, 35–50 wt% isopropanol, 10–20 wt% methyl ethyl ketone or ethanol, 5–10 wt% water, and 2–5 wt% anticorrosive pigment such as zinc phosphate and amorphous silica. The resin is dissolved in the alcohol-ketone phase before the acid-water phase is added under cooling at below 30 °C, because the exotherm and acid catalysis can cause partial acetal hydrolysis over extended storage. The primer is applied by air-assisted spray at a dry film thickness of 5–10 µm; a flash-off time of 10–15 min at 20–25 °C is used before overcoating with epoxy or polyurethane. Adhesion on degreased aluminium and steel is evaluated by ASTM D4541 pull-off testing; a minimum of 5 MPa with cohesive or mixed failure is generally specified for coil-coating lines, while ISO 2409 requires class 0 on the same substrate. Salt spray resistance after topcoating is assessed under ASTM B117; scribe creep below 2 mm after 250 h is a common internal acceptance criterion for architectural aluminium. The terminal component is a coil-coated aluminium or steel sheet used in building cladding, appliance cabinets, and automotive interior trim. The compliance matrix is provided in the table below.
| Regulatory/Standard Reference | Test Method | Acceptance Criterion |
|---|---|---|
| RoHS 2011/65/EU | IEC 62321-5 | Hexavalent chromium not intentionally added; Cr(VI) below the reporting limit of IEC 62321-5 |
| REACH SVHC screening | Supplier declaration and target analysis | No SVHC above 0.1 wt% in the dry film |
| Adhesion to metal | ASTM D4541 | ≥ 5 MPa |
| Cross-cut adhesion | ISO 2409 | Class 0 |
| Salt spray with topcoat | ASTM B117 | Scribe creep ≤ 2 mm after 250 h |
Field experience on coil-coating lines indicates that BX-5-containing primers can show viscosity increase during humid weather if the storage container is opened repeatedly; a nitrogen blanket or desiccant breather is required to maintain a moisture content below 0.5 wt% of the solvent phase. The primer is not suitable for direct contact with strong alkaline cleaners above pH 12 because the polyvinyl butyral film will re-emulsify and lose adhesion before topcoat application.
S-LEC BX-5 is blended into phenolic resin as a B-stage flexibilizer for paper-reinforced and glass-reinforced laminates, where its high molecular weight increases resin film toughness before cure and reduces the rigidity of the fully crosslinked phenolic network. The modifier is added at 5–15 phr based on phenolic solids and dissolved in an ethanol/toluene solution at 30–40 wt% solids before being mixed with the resole resin and flame retardant. Kraft paper or glass cloth is impregnated to a resin pickup of 45–55 wt%, then B-staged through a tunnel oven at 90–110 °C to a volatile content below 2 wt% as measured by oven drying. The prepreg is stacked and pressed at 150–170 °C under 5–15 MPa for 60–90 min. Flexural strength of the finished laminate is measured according to ISO 178, and notched Izod impact according to ASTM D256; the addition of PVB above 15 phr typically reduces flexural strength and increases water absorption, so the loading is capped at the point where a 24-hour water immersion in accordance with ISO 62 does not increase thickness beyond 1.5%. Electrical performance is assessed through comparative tracking index under IEC 60112 and flammability under UL 94; for FR-2 paper-based copper-clad laminates, the formulation is adjusted to maintain V-0 classification while retaining punching quality. The B-stage flexibilizer must not contain elevated acidic catalyst residues because these accelerate resole condensation and shorten prepreg shelf life below 7 days at 25 °C; the supplier lot is therefore titrated for acid number before scale-up. The terminal products are punched electrical insulators, appliance control boards, and cost-sensitive copper-clad laminates for consumer electronics. Published data for BX-5 in phenolic laminates is limited; the supplier grade should be evaluated for free ash and sodium content because residual inorganic material can degrade comparative tracking index in high-humidity service.
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S-LEC BX-5 is a polyvinyl butyral resin supplied by Sekisui Chemical Co., Ltd., identified within the S-LEC B series as a high-molecular-weight powder for solventborne binder systems. The polymer is produced by acetalization of polyvinyl alcohol with n-butyraldehyde; residual hydroxyl and acetyl functionalities determine the balance between adhesion to oxide surfaces and solubility in alcohol/ester/ketone solvent blends. Typical use areas include ceramic green-sheet tape casting for multilayer ceramic capacitors, solventborne printing inks, and corrosion-inhibitive wash primers. Lot-specific values for hydroxyl content, acetyl content, and solution viscosity appear on the manufacturer’s certificate of analysis; published data for this specific configuration is limited in the present compilation and should not replace a product specification.
Dissolution of S-LEC BX-5 is normally performed in a co-solvent blend of ethanol and toluene at a mass ratio between 60:40 and 50:50. The resin is charged into the vortex of a Cowles-type disperser operating at 5–10 m/s tip speed; the liquid temperature is initially held at 20–30 °C. In production vessels of 100–500 L, complete dissolution usually requires 60–120 min. The limiting boundary condition is solvent moisture. Water is a non-solvent for the butyral segment but associates strongly with residual hydroxyl groups; when the water content of the solvent blend exceeds 2 wt%, solution viscosity can increase by more than 15% relative to the anhydrous baseline. Recovered solvent loops should be dried to below 0.2 wt% water by Karl Fischer titration per ASTM E203 before resin charging.
After dissolution, the binder solution is passed through a depth filter with a nominal retention rating of 10–20 µm to remove gel particles and undissolved resin agglomerates. For ceramic tape-casting slurry, the filtrate is combined with ceramic powder under high-shear mixing in a planetary mixer equipped with a vacuum-deaeration stage; the final slurry viscosity is adjusted to 1000–5000 mPa·s at 10 s⁻¹, measured by cone-plate rheometer according to ISO 3219 or ASTM D4287. The slurry is cast through a doctor blade set to 50–250 µm gap onto a moving silicone-coated polyester carrier film. Drying zones are operated between 60 °C and 90 °C, with residence times of 2–8 min depending on solvent load and tape thickness. Residual solvent in the dried tape must remain below 1.5 wt%; higher values promote blocking on roll-up and reduce green density after lamination at 60–75 °C and 10–30 MPa.
Thermal debinding of BX-5-containing green tape is a two-stage process. Thermogravimetric analysis of polyvinyl butyral resins in this class under air at 10 K/min commonly shows the onset of weight loss near 240 °C, with combustion essentially complete by 450 °C. The critical temperature window lies between 200 °C and 350 °C; heating rates above 5 K/min through this interval can leave carbonaceous residue that degrades insulation resistance of the fired ceramic. A production profile typically maintains a debinding plateau at 350–400 °C for 1–4 h under flowing air at 3–6 chamber volumes per hour.
Binder loading is another boundary condition. In low-temperature co-fired ceramic tapes, the mass fraction of S-LEC BX-5 in the dried green sheet is typically kept between 5 wt% and 15 wt%. Below 5 wt%, green tensile strength falls below the 1.5–2.5 MPa range required for automatic blanking and handling; above 15 wt%, the debinding exhaust can overwhelm the oxidation capacity of the kiln and increase carbon defect rate. These limits shift with ceramic particle size distribution and should be confirmed by pilot runs.
Slurry de-aeration is equally critical. Dissolved gas in the S-LEC BX-5 solution delays vacuum draw and can stabilise microbubbles during doctor-blade coating. Pilot and production vessels usually apply a vacuum of 10–20 kPa absolute for 10–30 min after ceramic powder addition. Tapes cast from deaerated slurry show fewer pinholes and a more uniform green density profile across the web. Control limits for green density are commonly ±5% of the target value, measured by weight and thickness on punched coupons.
Production-scale tape-casting lines using S-LEC BX-5 have shown batch-to-batch molar mass variation can shift slurry viscosity by approximately ±10% at fixed solids. When such drift occurs, the preferred correction is solvent adjustment, not increased disperser speed; higher shear introduces air beyond 0.5 vol% and creates pinholes after drying and lamination. The same lines also exhibit a gradual increase in viscosity during extended slurry hold times above 24 h, caused by slow adsorption of PVB hydroxyl groups onto ceramic surfaces; this is managed by re-measuring viscosity per ASTM D4287 before each casting run and adding small amounts of anhydrous ethanol if the value exceeds the upper control limit.
When S-LEC BX-5 replaces a lower-viscosity PVB such as a BL or BM grade in a solventborne ink or coating, the primary observed changes are higher solution viscosity at equal resin solids, higher dried-film tensile strength, and reduced elongation at break. The viscosity increase is not linear with molecular weight; pilot dispersions typically require a solvent increase of 5–15 wt% to maintain the same rotational viscosity. The comparison below is intended for formulation screening rather than lot release.
| Parameter | Direction of change | Test method |
|---|---|---|
| Solution viscosity at equal solids | Higher; requires solvent increase of 5–15 wt% | ISO 2555 |
| Dried-film tensile strength | Higher | ASTM D638-14 |
| Elongation at break | Lower | ASTM D638-14 |
| Adhesion to soda-lime glass and aluminum | Comparable or higher depending on substrate | ASTM D3359-17 |
| Water vapour transmission rate of cast film | Comparable; pre-dry resin before compounding | ISO 15106-1 |
| Ash residue after incineration | Equivalent when ignited at 600 °C | ISO 3451-1:2019 |
In gravure ink formulation, BX-5 is typically used at 5–12 wt% of total ink in ethanol/ethyl acetate diluent. The final press viscosity is controlled to 20–100 mPa·s at 25 °C per ISO 2884-1. If press viscosity exceeds 120 mPa·s, solvent reduction may be necessary, but this lowers resin solids below the threshold for scuff resistance on coated paper. On a commercial gravure line with cylinder cell depth of 28–35 µm, filtering the BX-5 solution through a 5 µm absolute filter before ink letdown reduces doctor blade streaking and improves dot edge definition.
For flexographic applications, the resin’s molecular weight also influences reuse of press-return ink. Returned ink containing BX-5 retains fountain viscosity more stable than a lower-molecular-weight grade but is more sensitive to contamination from silicone defoamer residues. An inline viscosity controller with temperature compensation is recommended; process alarms are typically set at ±10% of the target viscosity range.
Plasticizer compatibility in printable film applications is also grade-sensitive. S-LEC BX-5 tolerates lower proportions of dibutyl phthalate before room-temperature tack develops; films formulated above 10 phr plasticizer may block in roll form at 35 °C. A lower-molecular-weight PVB can accept higher plasticizer levels without blocking but gives lower tensile strength. Formulators should evaluate blocking under 50 °C and 5 kPa for 24 h using a stacked-disc test.
Solvent compatibility of S-LEC BX-5 in wash-primer systems follows the general polyvinyl butyral solubility hierarchy: strong solvency in ethanol, n-propanol, ethyl acetate, and methyl ethyl ketone; limited solubility in toluene alone; insolubility in water and aliphatic hydrocarbons. When formulating a two-pack wash primer, the resin solution is kept separate from the acid activator until immediately before application. The activated solution has a finite pot life; gelation can occur more rapidly above 30 °C or at excessive phosphoric acid concentration. The process limits are discussed below.
Wash primers based on polyvinyl butyral and phosphoric acid are applied to steel and aluminum as thin pretreatment layers. S-LEC BX-5 provides film toughness and adhesion, while the acid component etches the metal surface and reacts with the hydroxyl groups of the resin. In a two-pack formulation, the base component is usually prepared at 10–20 wt% resin solids in ethanol or isopropanol, with a viscosity of 30–150 mPa·s at 25 °C per ASTM D2196. The activator contains phosphoric acid at 5–15 wt% based on the total mixed mass. Once mixed, the working pot is maintained below 30 °C; higher temperatures accelerate the reaction between hydroxyl groups and acid, leading to viscosity rise and gelation within 2–6 h instead of 8–12 h at 20 °C.
Application is typically by air-atomised spray gun with a fluid nozzle diameter of 1.2–1.8 mm and air pressure of 0.25–0.45 MPa. Dry film thickness is limited to 5–12 µm; thicker films can become brittle and lose intercoat adhesion with subsequent epoxy or polyurethane primers. The cured wash primer must pass cross-hatch adhesion per ASTM D3359-17 and salt-spray resistance per ISO 9227 when tested in a comparative system. Production lines using BX-5 in wash primers report that bath temperature is the dominant variable influencing pot life; a drop in spray booth temperature below 15 °C slows acid etching sufficiently to cause adhesion loss on cold-rolled steel.
Incoming lots of S-LEC BX-5 should be inspected for appearance, volatile matter, ash content, and solution viscosity. Powder colour should be uniformly white to pale yellow; dark particles indicate thermal damage or contamination. Volatile matter is determined on 2 g samples by drying to constant mass at 105 °C per ISO 3251. Ash content is determined by ignition at 600 °C per ISO 3451-1:2019; values above 0.1 wt% may indicate inorganic contamination from production equipment. Solution viscosity is reported on the certificate of analysis using a defined solvent blend and concentration; a common flow curve is measured by rotational viscometer per ISO 2555. Storage should be in closed, moisture-tight containers at 5–30 °C and relative humidity below 60%. At higher humidity, the powder can absorb moisture and form lumps that do not redisperse under normal shear. If lumps are observed, the lot should be pre-dried in a vacuum oven at 40–50 °C for 4–8 h before use.
| Framework | Applicability | Verification basis |
|---|---|---|
| EU chemical registration | Substance registration for industrial use | REACH (EC) 1907/2006 |
| Electrical/electronic equipment restrictions | Binder used in ceramic components; verify homogeneous material limits | RoHS 2011/65/EU |
| Food-contact adhesive or coating component | Not automatically cleared; verification required for specific use | FDA 21 CFR 175.105 |
| Quality management system | Manufactured under certified quality system | ISO 9001 |