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Anhui Liwei Chemical Co., Limited.

S-LEC BH-6

    • Product Name: S-LEC BH-6
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 511495
    Product Name S-LEC BH-6
    Product Type Polyvinyl butyral (PVB) interlayer film
    Thickness 0.76 mm
    Light Transmittance 88%
    Tensile Strength 20 MPa
    Elongation At Break 250%
    Tear Strength 60 kN/m
    Adhesion To Glass 15 N/25 mm
    Refractive Index 1.48
    Haze <1%
    Density 1.07 g/cm3
    Water Absorption <0.5%

    As an accredited S-LEC BH-6 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing S-LEC BH-6 is supplied in 25 kg sealed bags, with product identification and handling precautions printed on packaging.
    Container Loading (20′ FCL) S-LEC BH-6 loaded as 20′ FCL, packed in sealed bags on pallets, secured safely, kept dry.
    Shipping S-LEC BH-6 is a polyvinyl butyral resin shipped as solid pellets or powder in sealed moisture-proof bags, drums, or bulk containers. Keep dry, sealed, and away from heat and ignition sources. It is non-hazardous under normal transport, but avoid dust inhalation and protect packaging from physical damage.
    Storage Store S-LEC BH-6 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed when not in use to prevent water absorption and contamination. Avoid dust accumulation and static ignition. Under these conditions, the material remains stable for the recommended shelf life.
    Shelf Life Store in a cool, dry place away from light and moisture. Shelf life is typically 24 months from manufacture date in original sealed packaging.
    Application of S-LEC BH-6

    In multilayer ceramic capacitor tape casting, S-LEC BH-6 is used as the high-molecular-weight PVB binder because lower solution-viscosity grades produce insufficient green tensile strength during high-speed slitting and screen handling. The resin is first dissolved at 20–30 wt% solids in a 60:40 toluene:ethanol blend under closed agitation at 20–35°C, then post-added to a predispersed barium titanate slip that has been milled with a phosphate ester dispersant. Binder loading is normally maintained between 6 wt% and 12 wt% of the dry ceramic mass; values below 6 wt% produce edge cracking and tensile strength below 2 MPa in dried 100 µm tape, while values above 12 wt% increase the organic fraction that must be removed during air debinding at 250–450°C. On production-scale tape casters with doctor blade gaps of 200–400 µm, the slurry high-shear viscosity is generally held between 1,500 mPa·s and 4,000 mPa·s at 20 s⁻¹ per ISO 3219:2013, allowing deairing under 0.8 bar vacuum without boiling the solvent. Green tape is inspected for pinholes, thickness variation, and tensile properties across a 300 mm web; unsintered tensile strength and elongation are compared per ASTM D882-18 using 15 mm wide strips at a crosshead speed of 10 mm/min. Casting speed is typically 0.5–2.5 m/min, with drying ovens staged at 60–80°C and relative humidity controlled below 50% RH to prevent skin-over and trapped solvent. Because S-LEC BH-6 absorbs moisture from ambient air, bags are pre-conditioned in a dry room at 22–25°C and below 30% RH before weighing; opened drums exposed to more than 60% RH for more than 4 h require moisture testing by ASTM D6869-17 and, if water content exceeds 2 wt%, vacuum drying at 40°C before reuse. The terminal dielectric tapes are stacked, laminated, and printed with nickel internal electrodes, then fired under controlled oxygen partial pressure to produce MLCC capacitors with layer thickness down to 1 µm.

    ComponentTypical range in high-solids MLCC slipProcess consequence at lower boundaryProcess consequence at upper boundary
    S-LEC BH-6 dry binder6–12 wt% of BaTiO₃Green tape edge tear strength below 2 MPa; slitting scrap increasesLonger debinding plateau; higher risk of carbon residue after air firing
    Phosphate ester dispersant0.5–2.0 wt% of BaTiO₃Slurry yield stress rises; casting streaks appearFired dielectric insulation resistance may decrease
    Dioctyl phthalate plasticizer0–5 phr of binderTape becomes brittle at low humidityGreen density decreases; condenser oven fouling increases
    Resin solution concentration20–30 wt% in toluene:ethanol 60:40Filtration rate drops due to high solution viscosityCold-flow risk increases in storage below 10°C

    What Limits Binder Burnout Throughput in Nitrogen-Fired LTCC Tape?

    Low-temperature co-fired ceramic tape lines running gold or silver conductors face a narrower debinding window than air-fired MLCC because the furnace atmosphere does not fully oxidize PVB decomposition products. S-LEC BH-6 in LTCC tape is compounded with a crystallizing glass and alumina filler at a total solids loading of 40–60 vol%, with the PVB binder fraction typically 8–14 wt% of the inorganic powder. After tape casting and blanking, individual layers are laminated at 70–90°C under 10–20 MPa; the laminated panel is then fired on a setter plate at 850°C for 30–60 min. The throughput-limiting zone is not the peak firing hold but the 250–450°C interval, where side-chain elimination of butyraldehyde and condensable plasticizer fractions can exceed the furnace exhaust extraction rate. In nitrogen atmospheres with residual oxygen below 20 ppm, retained carbon above 0.1 wt% produces gray or black core discoloration and can raise buried inductor leakage current after 96 h of 85°C/85% RH biased humidity testing. Ramp rates through this interval are therefore typically limited to 0.5–2.0°C/min; for stacks thicker than 1.5 mm, the lower ramp boundary is required because gas diffusion length scales with the square of the unfired stack thickness. A plateau of 60–120 min at 350°C is inserted on production lines when the furnace has fewer than four independent heating zones. Before release, printed and laminated panels are dried at 70–80°C for 12–24 h to reduce residual solvent below 0.5 wt% of binder mass; insufficient drying shifts TGA onset and creates gas bubbles between layers during the 250–350°C ramp. Furnace profiling uses sacrificial panels at 3-inch grid spacing across the belt to verify that part temperature does not exceed the 2.0°C/min ramp limit in any zone. Outgassing behavior is qualified by thermogravimetric analysis with evolved gas detection per ISO 11358-1:2014, and pre-fire tape adhesion is checked by ASTM D903-98(2017) peel testing on laminated coupons. Published burnout kinetic data for this specific grade in pure nitrogen is limited; production release therefore relies on post-fire ion chromatography for residual carbonate rather than assuming complete oxidation from a single TGA curve. Terminal LTCC components include hermetic RF modules, multilayer inductors, and ceramic sensor housings where fire-through carbon would compromise Q factor and long-term bias stability.

    When Thick-Film Silver Paste Squeegee Pressure Drops Below 0.4 MPa

    For fine-line thick-film silver conductors on 96% alumina substrates, S-LEC BH-6 is dissolved in a high-boiling solvent mixture of terpineol and butyl carbitol acetate at 8–15 wt% resin solids, then milled into a paste with spherical silver powder at 85–90 wt% total solids and a glass frit content of 2–4 wt% of the metal. The paste is screen-printed through a 325-mesh stainless-steel screen with 20–25 µm emulsion thickness. Production-scale printers maintain squeegee pressure between 0.4 MPa and 0.7 MPa with a flood bar speed of 60–120 mm/s. Below 0.4 MPa, the paste fails to release from the screen openings onto the substrate; the resulting deposited film shows starved edges and dry opens after solvent evaporation at 150°C. Above 0.8 MPa, mesh yield increases and the resin phase may be forced into substrate pores, leaving a silver-rich surface that fires with poor solder joint integrity. After printing, parts are dried at 120–150°C for 10–15 min and fired in air at 850°C for 10 min at peak. Wire bond pull strength is measured per MIL-STD-883K Method 2011.9; a fired conductor film thickness of 8–12 µm is typically obtained from a single print pass. PVB-based paste is not recommended for nitrogen-fired profiles below 500°C unless the furnace includes an air pre-oxidation zone of at least 15 min above 350°C; otherwise interfacial carbon residue reduces wire bond adhesion and promotes solder leach in subsequent hybrid assembly. The terminal applications are alumina hybrid circuits and sensor packages where fired film line resolution and ultrasonic bonding reliability define yield.

    Metal pretreatment lines use S-LEC BH-6 as the film-forming binder in single-pack acid-catalyzed wash primers because the polymer tolerates the low pH of phosphoric acid while bonding to lightly abraded steel and aluminum. A production-scale primer formulation includes 8–15 wt% resin solids, 3–6 wt% phosphoric acid at 85%, 0.5–2.0 wt% zinc phosphate or a zinc-free corrosion inhibitor, and a solvent blend of isopropanol, n-butanol, and xylene at 70–85 wt% total volatiles. The acid etches the metal surface and reacts with hydroxyl groups on the PVB chain, forming phosphate esters that raise dry-film pull-off adhesion on hot-rolled steel from roughly 2–3 MPa to 5–8 MPa as measured by ISO 4624:2016. The primer is spray-applied at 10–15 µm dry film thickness and overcoated within 4–8 h to avoid intercoat adhesion failure from solvent entrapment. Spray booths are held at 20–30°C and 40–60% RH; below 40% RH, the solvent blend flashes too quickly and can trap air at the steel profile root. Airless spray tips of 0.009–0.013 inch are used on structural steel, while conventional HVLP guns are preferred for rail car interior frames because overspray can be controlled in confined spaces. Because the formulation is acid-catalyzed, amine-based curing agents must not be combined with this primer in the same line unless the booth atmosphere is segregated; amine contamination causes precipitation of the PVB-phosphate complex and a measurable drop in salt-spray resistance. Chrome-free versions formulated to comply with REACH Annex XVII restrictions on chromium(VI) and RoHS Directive 2011/65/EU are specified for electrical enclosure pretreatment where lead and hexavalent chromium are excluded. Terminally, the primer is used under epoxy and polyurethane topcoats on agricultural equipment, rail car interior frames, and steel superstructures; edge protection and field-applied repair touch-up are stronger with BH-6-based primers than with low-molecular-weight PVB grades.

    Compliance requirementStandard or regulationApplication condition for BH-6 wash primer
    Chromium(VI) contentREACH Annex XVII entry 47Chrome-free zinc phosphate or zinc-free inhibitors; dried film below 0.1 wt% Cr(VI)
    Heavy metals in electrical/electronic equipmentRoHS 2011/65/EU Annex IIPb, Cd, Hg below 1000 ppm; Cd below 100 ppm
    Pull-off adhesionISO 4624:20165–8 MPa on hot-rolled steel after 24 h dry
    Neutral salt spray resistanceISO 9227:2017500 h with 2–3 mm scribe creep on cold-rolled steel
    Solvent resistanceASTM D5402-19100 double rubs with methyl ethyl ketone without substrate exposure

    Flexographic Ink Resin Compatibility and Heat-Seal Window

    During lamination of surface-printed polypropylene and polyester flexible packaging, S-LEC BH-6 is used as a co-binder with nitrocellulose and polyurethane to balance adhesion and heat-seal release. The PVB fraction is typically 5–12 wt% of total ink resin solids; below 5 wt%, ink adhesion to corona-treated OPP at surface energy 38–42 mN/m drops below acceptable tape-off limits, while above 12 wt% the dried ink can block during rewind at 35–40°C warehouse temperatures. The resin is pre-dissolved in ethyl acetate and ethanol at 15–20 wt% solids before letdown; final ink viscosity is adjusted to 25–35 s on a No. 3 Zahn cup at 25°C. During downstream jaw sealing of the printed web to LDPE blown film at 110–130°C, the PVB phase softens sufficiently to prevent delamination at the seal interface. Heat-seal strength is assessed per ASTM F88/F88M-21 and is generally maintained above 1.5 N/15 mm in the 100–120°C seal range. Waterborne alkaline inks are not compatible with this resin if added directly; phase separation occurs unless cosolvent content is maintained above 20 wt% of the total solvent. For food-contact printed packaging, the finished ink must comply with 21 CFR 175.300 resinous and polymeric coatings conditions when the print is on the outer surface with a functional barrier; residual solvent is controlled below 50 mg/m² by ISO 11890-2. The terminal printed laminates include confectionery, snack, and hygiene packaging where low odor and fast solvent release are mandatory.

    Temporary Masking Coatings for Chemical Milling and Anodizing Lines

    For chemical milling of 2024-T3 clad aluminum, a PVB maskant formulated with S-LEC BH-6 is dissolved at 15–20 wt% solids in methyl ethyl ketone and ethanol, with dibutyl phthalate added at 10–15 phr on resin solids to retain elongation after drying. The maskant is spray-applied at 200–400 µm wet film thickness and dried to a continuous film that must withstand immersion in 10–15 wt% sodium hydroxide at 70–90°C for 30–60 min without lifting from scribed edges. Low-number-average PVB grades fail by adhesive peeling after approximately 20 min in high-alkali baths; the higher chain length of BH-6 maintains tensile strength above 3 MPa after 48 h immersion at 25°C in 5 wt% sodium hydroxide in comparative laboratory screening. Dried maskant films are inspected for pinholes after application by high-voltage holiday detection at 2–5 kV; pinholes are touched up with brushable maskant to prevent etch pits in the aluminum. Maskant removal after milling uses methyl ethyl ketone wiping or solvent immersion; peel residues on clad aluminum are evaluated by water break-free surface inspection per ASTM F22-21. The compound is not recommended for masking stress-relieved polycarbonate or acrylic because the methyl ethyl ketone carrier attacks these substrates; reformulation to a low-aromatic alcohol blend is required for plastic optics. Published data for this specific BH-6 maskant formulation is limited to comparative laboratory screening rather than full aerospace qualification; therefore, each production lot is batch-tested for alkali immersion adhesion before release. Terminal parts include wing skins, fuselage pockets, and anodized structural brackets where the maskant must protect machined surfaces from alkaline attack and prevent etch-out beyond the scribed boundary.

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    Certification & Compliance
    More Introduction

    S-LEC BH-6 is a high-polymerization-degree polyvinyl butyral resin supplied by Sekisui Chemical Co., Ltd. The material belongs to the BH series of the S-LEC product family and is positioned above lower-viscosity BL and BM grades. PVB of this class is produced by acid-catalyzed acetalization of polyvinyl alcohol with n-butyraldehyde; the polymer retains a controlled residual hydroxyl fraction and a smaller acetyl fraction after condensation. The hydroxyl groups provide adhesion to glass, aluminium, ceramic, and metal substrates, while the butyral groups provide solubility in oxygenated solvent blends, plasticizer compatibility, and toughness. The resin is generally supplied as a free-flowing powder or granular solid; bulk density of commercial high-viscosity PVB powder measured under ISO 60 normally lies between 0.20 g/cm³ and 0.45 g/cm³. Lot-specific values for S-LEC BH-6 must be taken from the certificate of analysis because moisture content and particle-size distribution influence bulk density.

    Moisture handling is a critical boundary condition. PVB is hygroscopic, and equilibrium moisture above 0.5 wt% can introduce bubble defects and viscosity drift during dissolution or melt processing. When ambient relative humidity exceeds 60 %, pre-drying in a vacuum oven at 40–50 °C for 4–8 h or in a desiccant dryer with a dew point below -30 °C is commonly applied. If the resin is stored in opened bags at 25 °C and 70 % relative humidity for more than 24 h, moisture uptake may exceed the recommended limit.

    The primary industrial use of S-LEC BH-6 is as a high-strength organic binder in non-aqueous ceramic tape casting slips. In a typical barium titanate or alumina system, the solvent mixture consists of ethanol and toluene or ethanol and methyl ethyl ketone. The high molecular weight of BH-6 reduces binder migration during drying and increases green tape strength, but it also increases solution viscosity and requires a separate predissolution stage. A production-scale predissolution step is usually executed in a jacketed high-shear mixer at 40–50 °C and 1,500–3,000 rpm for 2–4 h. The resulting binder solution is filtered through a 25–50 μm screen before ceramic powder addition. This procedure prevents undissolved gel particles from producing surface defects in tape cast with a doctor blade gap of 100–300 μm.

    Why Does the Viscosity Gap Between BH-6 and BM Series Resins Matter in Production?

    The elevated solution viscosity of S-LEC BH-6 is directly related to its higher average molar mass. In comparative formulations at equal solids loading, BH-6 produces a higher Brookfield viscosity at 20 °C and a more pronounced shear-thinning index than BM series resins. Viscosity can be measured according to ISO 2555, but a cone-and-plate rheometer with a shear-rate sweep from 0.1 s⁻¹ to 100 s⁻¹ gives better differentiation of lot-to-lot variation. Production batches are often adjusted by reducing solids loading by 2–5 wt% rather than by adding additional strong solvent, because excess solvent increases drying load and can lower final ceramic tape density.

    At equal binder content, high-molecular-weight PVB films typically exhibit higher tensile strength than lower-viscosity grades. Unplasticized solvent-cast PVB films measured according to ISO 527-2 often show tensile strength above 25 MPa for high-polymerization resins, while low-viscosity grades may fall below 18 MPa. Elongation at break usually moves in the opposite direction. For S-LEC BH-6, the exact value depends on hydroxyl content, plasticizer type, and solvent drying conditions. The higher strength is useful in ceramic green tape handling, where a 50–100 μm tape must survive slitting, punching, and lamination without edge cracking.

    Batch-to-batch variation in PVB resin hydroxyl content is typically controlled within ±1 wt%. For S-LEC BH-6, the certificate of analysis should be checked against the internal specification before dissolution because a shift of 2 wt% hydroxyl content changes adhesion and solubility. In a continuous doctor-blade line, such a shift can alter slurry viscosity by more than 10 % at constant solids.

    In high-solids ceramic slip preparation, the dissolution sequence changes dispersion quality. When S-LEC BH-6 is added directly to a slip containing ceramic powder and dispersant, the polymer can compete with the dispersant for surface adsorption sites on oxide particles. The result may be a yield-stress increase or flocculation. The preferred sequence is to combine solvent, plasticizer, and BH-6 first, then add dispersant and ceramic powder under high shear. A three-roll mill or bead mill with 0.6–1.0 mm zirconia media is used for ceramic dispersion at residence times from 5 min to 20 min. Final slurry viscosity is typically adjusted to 2,000–5,000 mPa·s at 25 °C using a spindle viscometer at 20 rpm. This viscosity window corresponds to stable doctor-blade casting at speeds from 0.5 m/min to 2.0 m/min.

    Thermal Decomposition and Binder Burnout in High-Density Ceramic Tapes

    PVB resins begin to decompose near 200 °C, and the high molecular weight of BH-6 requires staged thermal treatment to achieve clean burnout. In a multi-zone belt furnace, a typical profile uses a first zone at 180–220 °C to remove residual solvent without forming a surface skin, a second zone at 320–350 °C for oxidation of the butyral backbone, and a third zone at 450–500 °C in flowing air at 50–100 L/min. The heating ramp between zones is limited to 0.5–1.0 °C/min to avoid delamination and blistering in multilayer ceramic capacitors. Residual carbon is measured by combustion analysis and should remain below 0.05 wt% for nickel-electrode compatibility. Published data for S-LEC BH-6 in every specific ceramic formulation is limited; therefore the burnout window must be validated for each ceramic powder and plasticizer loading.

    Processing above 180 °C in hot-melt compounding requires antioxidant stabilization. A twin-screw extruder with an L/D ratio of 30:1 to 44:1 and barrel temperatures profiled from 120 °C to 170 °C is used for plasticized PVB compounds. The addition of 0.1–0.5 wt% hindered phenolic antioxidant retards chain scission and discoloration. Amine-based additives, particularly primary aliphatic amines, are incompatible at elevated temperature because they can promote yellowing and crosslinking; their use in S-LEC BH-6 melt formulations should be screened at the intended production concentration.

    Plasticizer migration kinetics in polymer matrices are slower for S-LEC BH-6 because the longer chains increase the diffusion path and reduce free-volume concentration. In laminated glass interlayer applications, this slows edge migration and maintains impact resistance over a wider temperature window. Diffusion coefficients for phthalate plasticizers in high-viscosity PVB at 60 °C are of the order of 1 × 10⁻¹² m²/s to 1 × 10⁻¹¹ m²/s; values for low-viscosity grades can be significantly higher. These differences influence long-term performance in safety glass and photovoltaic encapsulant applications.

    When the Solvent Matrix Moves from Ethanol/Toluene to Glycol Ether Acetate

    Dissolution behaviour changes significantly when the solvent matrix shifts from ethanol/toluene to ester or glycol ether acetate systems. In ethyl acetate/ethanol or propylene glycol monomethyl ether acetate, high-viscosity PVB resins such as S-LEC BH-6 can require 1.5 to 2.5 times longer dissolution than in ethanol/toluene at 25 °C. A high-shear rotor-stator mixer operating at a tip speed of 10–20 m/s may be needed to achieve complete solubilization within 90–120 min. For gravure and flexographic ink applications, the higher viscosity improves pigment wetting and reduces misting, but the final press viscosity must be reduced with a glycol ether solvent or low-viscosity PVB co-resin. The solvent blend also changes the evaporation profile; an ester-based system with a relative evaporation rate above 3.0 compared with n-butyl acetate can cause premature skinning on the print cylinder if press speed is below 50 m/min.

    Compatibility with alkyd, epoxy, and acrylic resins in coating formulations is limited by solvent polarity and hydrogen-bonding capacity. S-LEC BH-6 tends to phase-separate from highly nonpolar acrylic resins in low-oxygen solvent blends; formulation stability should be checked by a ternary solubility map before scale-up. The addition of 5–10 wt% of a high-boiling glycol ether based on total solvent can extend open time in dip-coating operations where wet film thickness is 20–50 μm.

    Relative to ethyl cellulose, PVB burns out more cleanly but is less tolerant of purely aliphatic solvents. Relative to acrylic binders, PVB has better adhesion to glass and metal but lower resistance to continuous service above 120 °C. The selection of S-LEC BH-6 over alternative PVB grades depends primarily on the minimum solution viscosity required for the coating operation and the allowable solvent demand.

    For electrical and electronic applications, the resin is evaluated under applicable material declaration rules. A homogeneous material screening by X-ray fluorescence and wet chemistry is still required to confirm that cadmium, lead, mercury, hexavalent chromium, PBB, and PBDE are below the maximum concentration values of EU Directive 2011/65/EU. Under REACH, PVB as a polymer may be exempt from registration under Article 2(9), but imported monomers and any residual n-butyraldehyde are subject to the registration and restriction framework. Food-contact use requires application-specific clearance; unmodified S-LEC BH-6 should not be assumed to comply with FDA 21 CFR 175.300 or national food-contact provisions without a formal letter of compliance.

    ParameterReference methodEvaluation in production
    Bulk densityISO 600.20–0.45 g/cm³ depending on particle-size distribution
    Solution viscosityISO 2555Compare lot-to-lot at fixed solids and solvent; use a control chart for BH-6 acceptance
    Tensile strength of cast filmISO 527-2High-viscosity PVB typically above 25 MPa for unplasticized film; not a specification for all applications
    Glass transitionISO 11357-260–70 °C for unplasticized PVB; plasticized material lower
    Ash contentISO 3451-1Below 0.5 wt% after burnout unless inorganic anti-block is added
    RoHS substancesDirective 2011/65/EUNo intentionally added restricted substances above thresholds; confirm by XRF screening

    In structural adhesive primer applications, S-LEC BH-6 may be formulated with silane coupling agents and epoxy resins to enhance adhesion to glass and aluminium. The addition of 1–2 wt% silane based on total solids improves wet adhesion, but the silane must be added after all water is removed because moisture hydrolyzes the silane and can gel the PVB solution. A cross-cut adhesion test according to ISO 2409 on degreased glass after 24 h at 23 °C and 50 % relative humidity typically yields classification 0 or 1 for a properly formulated primer. After 72 h of water immersion at 23 °C, the same system may show a two-class drop if adhesion control additives are insufficient. This operational boundary defines the use of S-LEC BH-6 in moisture-sensitive bonding applications.

    Above approximately 12–15 wt% binder based on ceramic powder, slurry viscosity can exceed 10,000 mPa·s at 25 °C and require vacuum de-airing under 50–100 mbar before casting. If viscosity is not reduced by solvent addition, the high-shear mixing step itself may raise slurry temperature above 35 °C and cause solvent evaporation, shifting solids content.