| HS Code | 853728 |
| Chemical Name | Polyvinyl Butyral |
| Cas Number | 63148-65-2 |
| Physical Form | White free-flowing powder |
| Glass Transition Temperature | 68-72 °C |
| Hydroxyl Content | 18-23 wt% |
| Butyral Content | 75-80 wt% |
| Acetate Content | 0-3 wt% |
| Viscosity | 20-200 mPa·s (5 wt% ethanol solution, 20 °C) |
| Weight Average Molecular Weight | 40,000-200,000 g/mol |
| Solubility | Soluble in alcohols, glycol ethers, ketones, and esters; insoluble in aliphatic hydrocarbons |
| Thermal Decomposition Temperature | >250 °C |
| Acid Value | ≤0.5 mg KOH/g |
| Softening Point | 60-80 °C |
As an accredited PVB Resin for Reprographic Coatings & Specialty Toners factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg sealed fiber drums with inner polyethylene liner, ensuring moisture protection and safe handling. |
| Container Loading (20′ FCL) | Load 20′ FCL with PVB resin in sealed drums, palletized, secured, moisture-protected, and properly labeled for safe transport. |
| Shipping | Ship PVB Resin in sealed, moisture-resistant polyethylene-lined bags or fiber drums on palletized, stretch-wrapped units. Keep dry and away from ignition sources during transit. Use standard dry containers or covered trucks; material is non-hazardous under ADR/IMDG for normal handling. Protect from prolonged heat and humidity to preserve product quality. |
| Storage | Store PVB resin in a cool, dry, well-ventilated area away from heat, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid oxidative conditions and strong oxidizing agents. Recommended storage temperature is typically below 25°C (77°F). Use proper labeling and first-in, first-out rotation to maintain quality and stability. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored unopened, dry, and below 30°C. Protect from moisture and heat. |
At a melt-kneading throughput of 18–25 kg/h through a co-rotating twin-screw extruder with L/D 44 and barrel temperatures 95–135 °C, PVB functions as either a co-binder or sole binder in electrophotographic toners. When used as a co-binder to modify polyester or styrene-acrylic systems, the addition ratio is 4–8 wt% of total toner mass; when used as the sole binder in low-temperature fusing grades, the loading rises to 52–68 wt% of total toner mass. The compounding sequence includes pre-drying PVB at 45–50 °C for 8 h to reduce residual moisture below 0.3 wt%, dry blending, melt-kneading at a residence time of 25–40 s, cooling, coarse crushing, jet milling to a volume-median particle size of 6.5–8.0 µm, air classification, and surface treatment with hydrophobic silica at 0.8–1.2 wt%. Compliance for finished cartridges includes RoHS Directive 2011/65/EU Annex II, REACH Regulation EC 1907/2006, and substance declaration according to IEC 62474:2020; page-yield verification follows ISO/IEC 19752:2017 for monochrome systems and ISO/IEC 19798:2017 for color systems. On production lines, barrel temperatures above 180 °C during shutdown intervals of 3–5 min initiate thermal decomposition and color formation, causing melt flow index to shift outside the specification measured by ISO 1133-1:2022; PVB grades with hydroxyl content above 21.5 mol% increase moisture uptake and produce triboelectric charge drift of ±4 µC/g between 50% RH and 80% RH. Terminal finished product types include specialty monochrome cartridges for high-speed enterprise document printing, remanufactured cartridges, and low-odor desktop printer toners.
On a ring-coating line for organic photoconductor drums, PVB is the film-forming binder in a solvent-borne undercoat dispersion applied to sandblasted A3003 aluminum cylinders with surface roughness Ra 0.18–0.25 µm. The coating liquid contains PVB solids at 6–12 wt% relative to total liquid mass, and the binder-to-anatase TiO₂ filler ratio is maintained between 1:0.8 and 1:1.2 by mass; a polyether-modified silane adhesion additive is limited to 0.3–0.6 wt% of solids. Processing consists of bead milling at 1,800–2,200 rpm with 0.6–0.8 mm zirconia media for 20–40 min, dilution to 12–25 cP at 20 °C, filtration through 0.2 µm absolute media, and dip or ring coating at draw speeds of 1.2–1.8 m/min before forced-air drying at 80–110 °C to a dry film thickness of 2–5 µm. Compliance is documented under IEC 62474:2020 and RoHS Directive 2011/65/EU Annex II; adhesion is qualified by cross-cut tape pull according to ASTM D3359-17, and damp-heat resistance is tested at 40 °C/90% RH for 500 h under IEC 60068-2-78:2012. In practice, adhesion loss occurs when acetal content falls below 69 mass% or when the substrate is not pre-dried at ambient relative humidity above 60%; film cracking appears below 2 µm dry thickness during drum thermal cycling, and metal acetylacetonate additives cause premature crosslinking through residual hydroxyl groups at drying temperatures above 100 °C. Terminal finished product type is the organic photoconductor drum assembly used in laser printers, multifunction devices, and digital copiers.
At 23 °C and 50% RH, a dielectric paper coating formulated with PVB as the majority binder exhibits surface resistivity above 1013 Ω/sq when tested according to ASTM D257-14, which is required for electrostatic plotting media. In this application, PVB constitutes 70–85 wt% of the total binder system, blended with 15–30 wt% styrene-acrylic copolymer; the total binder-to-pigment ratio ranges from 1:1.5 to 1:2.0 using calcined clay or precipitated calcium carbonate, while PVB solids represent 8–15 wt% of the overall coating formulation. Blade coating on 80–120 g/m² base paper runs at 150–250 m/min, followed by two-zone drying at 95–135 °C and soft-nip calendering at 70–90 °C to maintain Parker PrintSurf roughness below 1.4 µm. The terminal finished product type is a dielectric paper roll for wide-format electrostatic plotters and technical document reproduction. Compliance is documented under REACH Regulation EC 1907/2006 and EU Directive 94/62/EC on packaging and packaging waste; electrostatic dissipation properties in the production environment are evaluated under IEC 61340-5-1:2016. An operational limit observed on blade coating lines is that PVB batches with acetal content above 74 mass% generate rapid solvent release and edge streaks unless the coating color is pre-sheared at 800–1,200 s⁻¹ for 20–30 min; this pre-shear stabilizes viscosity and prevents blade chatter.
PVB is incorporated into the heat-resistant backcoat layer of thermal transfer ribbons to bind slip agents to 4.5 µm polyester film while preventing hot-melt ink from sticking to the printhead. The dry backcoat contains PVB solids at 12–18 wt% relative to total dry solids, blended with 6–10 wt% silicone-modified acrylic, 0.8–1.2 wt% amino-functional silane, and the remainder heat-resistant filler; the lacquer is applied by gravure coating with cylinder cell depth 12–18 µm at 180–250 m/min, and dried at 90–110 °C to a dry film thickness of 0.5–1.0 µm. Terminal finished product types are thermal transfer ribbons for barcode labels, wristbands, and laboratory slide cassettes. Compliance is managed under IEC 62474:2020 and RoHS Directive 2011/65/EU Annex II; linear bar code print quality is verified according to ISO/IEC 15416:2016, and two-dimensional symbol verification follows ISO/IEC 15415:2011. The operational boundary is set by hydroxyl content in PVB: above 21.5 mol%, moisture uptake at 70% RH leads to ribbon blocking on unwinding, while a dry film thickness below 0.5 µm produces backcoat failure within the first 300–500 linear meters of ribbon travel and leaves residue on the ceramic heater edge.
Unlike pulverized styrene-acrylic MICR toners, a formulation based on PVB as a co-binder improves adhesion of the fused magnetic layer to sort-type and check-grained paper while maintaining magnetite loading. The MICR toner contains 40–55 wt% acicular magnetite, 6–12 wt% PVB relative to total toner mass, 1–3 wt% charge control agent, and 2–5 wt% wax; the remaining binder is a polyester or styrene-acrylic with softening point 105–125 °C. Compounding uses a twin-screw extruder with L/D 48 and hardened screw elements at barrel temperatures 100–130 °C; the cooled extrudate is jet-milled and air-classified to a volume-median particle size of 8.0–9.5 µm before blending with 0.6–1.0 wt% hydrophobic silica. The terminal finished product type is a MICR toner cartridge used in bank check printing and remittance processing. Signal level and placement are verified according to ANSI X9.100-160-1, while restricted-substance compliance follows RoHS Directive 2011/65/EU Annex II and REACH Regulation EC 1907/2006. A production-scale failure mode is screw and barrel wear accelerated by magnetite at 40–55 wt%; nitrided barrel liners on L/D 48 extruders show measurable wear after 900–1,200 h, shifting melt viscosity and reducing image density. PVB containing more than 0.5 wt% residual water must be pre-dried at 45–50 °C for 8–12 h before extrusion to avoid hydrolysis and tribocharge instability.
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Polyvinyl butyral resin supplied as model PVB-RC 60 T is a low-gel, hydroxy-functional binder manufactured by acetalization of polyvinyl alcohol with n-butyraldehyde. The resin is controlled to residual polyvinyl alcohol 18.0–21.0 wt%, residual polyvinyl acetate ≤ 2.5 wt%, and solution viscosity 50–70 mPa·s measured as a 10 wt% solution in anhydrous ethanol at 20 °C by rotational viscometry according to ASTM D2196-20. The corresponding weight-average molecular weight is not reported as an absolute light-scattering value because published data for this exact configuration are limited; batch release therefore uses viscometric molecular weight as the control parameter. Glass transition temperature determined by differential scanning calorimetry is 68–72 °C per ISO 11357-2:2020 at a heating rate of 20 K/min. Volatile content is ≤ 2.0 wt% by ISO 3251:2019, acid value is ≤ 1.0 mg KOH/g by ISO 2114:2000, and sulfated ash is ≤ 0.1 wt% by ISO 3451-1:2019. Chemical Abstracts Service registry number is 63148-65-2, and bulk density is 0.35–0.55 g/cm³ by ISO 60:1977.
Solvent-borne reprographic coatings are prepared with the resin at 8–15 wt% solids in an 85:15 w/w ethanol–methyl ethyl ketone blend. High-shear dissolution is conducted at 20–25 °C using a cowles disperser with tip speed 5–10 m/s; local overheating above 40 °C increases microgel count in the filtered solution. The lacquer is applied to 125 µm corona-treated polyethylene terephthalate at wet film thickness 12–30 µm by slot-die or reverse-gravure coating. A three-zone forced-air oven with zone temperatures 60 °C, 85 °C, and 105 °C removes residual solvent to ≤ 300 ppm total residual solvents as measured by headspace gas chromatography. The resulting clear topcoat shows haze ≤ 1.5% according to ASTM D1003-21, König hardness 120–150 s by ISO 1522:2022, and cross-cut adhesion to polyester of class 0–1 according to ISO 2409:2020. The hydroxyl group density of the resin provides adhesion without an additional primer; this is a measurable difference from low-hydroxyl acrylic binders used in the same coating position.
Dry specialty toner compounding uses the resin as the primary melt binder and as a polar charge-control substrate. A typical formulation contains 45–55 wt% PVB-RC 60 T, 35–45 wt% magnetite, 1–2 wt% metal-azo charge-control agent, and 0.5–1.5 wt% fumed silica. Melt mixing is performed on a co-rotating twin-screw extruder with L/D 40:1, barrel zones from 90 °C at feed to 150 °C at die, and screw speed capped at 250 rpm. Higher residence time or localized shear above 180 °C promotes acetal hydrolysis and darkening. The cooled extrudate is pre-crushed and jet-milled to volume-median particle size 6.5–8.0 µm as determined by laser diffraction per ISO 13320:2020; classifier yield in the target band is expected to be ≥ 85%. Against ferrite carrier, the resin develops negative triboelectric charge; after 30 min roll-mill activation, charge-to-mass ratio falls between 18–25 µC/g when measured by blow-off method with 0.5 wt% metal-azo charge-control agent. The minimum fixing temperature on a benchtop fusing rig is 135 °C and hot offset onset is 175 °C at nip pressure 200 g/cm² and process speed 40 mm/s. Because published capillary rheometry data for this specific configuration are limited, melt-viscosity curves should be verified on a capillary rheometer with a 1 mm × 20 mm die before production.
On reprographic film coating lines, the dissolved resin is filtered through 5 µm absolute-rated polypropylene depth filters directly upstream of the coating die. Solutions stored for more than 72 h at 25 °C in unsealed vessels show microgel formation and viscosity drift; dry powder storage is 24 months in moisture-barrier packaging at ≤ 30 °C and ≤ 60% RH. If exposure to RH > 60% occurs, the powder is pre-dried at 60 °C for 4 h before melt compounding or dissolution. The resin is incompatible with concentrated mineral acids, strong oxidizers, and long-chain primary amines above 180 °C during melt processing; these materials accelerate acetal hydrolysis, colour shift, and charge-control interference. The resin should not be stored in open containers near low-molecular-weight ketones and high humidity because moisture uptake shifts solution viscosity and final film clarity.
Residual hydroxyl content is the main specification variable controlling solution viscosity, adhesion, and toner charging. At the lower limit of 18.0 wt% residual polyvinyl alcohol, dissolution in 95% ethanol at 25 °C reaches clarity within 45 min; at the upper limit of 21.0 wt%, dissolution extends to 90 min and viscosity rises nonlinearly. This band is narrower than general-purpose PVB grades, which may span 11–25 wt% residual polyvinyl alcohol, and it prevents large batch-to-batch shifts in triboelectric charging and fusing latitude. Residual polyvinyl acetate is controlled at ≤ 2.5 wt%; each 1 wt% increase in residual acetate lowers glass transition temperature by approximately 2–3 °C and raises blocking tendency in stored toner. The low-gel character of the product is monitored by filtration ratio through a 5 µm absolute filter; a filtration ratio above 1.3 indicates microgel formation and is cause for lot rejection in reprographic coating service.
| Property | Specification | Test method |
|---|---|---|
| Residual polyvinyl alcohol | 18.0–21.0 wt% | ASTM D1396-92(2019) |
| Residual polyvinyl acetate | ≤ 2.5 wt% | ASTM D1396-92(2019) |
| Solution viscosity | 50–70 mPa·s at 10 wt% in ethanol, 20 °C | ASTM D2196-20 |
| Volatile content | ≤ 2.0 wt% | ISO 3251:2019 |
| Acid value | ≤ 1.0 mg KOH/g | ISO 2114:2000 |
| Sulfated ash | ≤ 0.1 wt% | ISO 3451-1:2019 |
| Glass transition temperature | 68–72 °C | ISO 11357-2:2020 |
| Particle size, Dv90 | ≤ 200 µm | ISO 13320:2020 |
The suffix 60 in the product designation corresponds to the midpoint of the 50–70 mPa·s solution viscosity band; the suffix T indicates the low-gel toner grade with reduced coarse fraction. Incoming lot acceptance includes solution colour after filtration, with an acceptance limit of APHA ≤ 100, and film haze as a secondary lot-release check. Batch records on production-scale coating lines show that filtration pressure rise across the 5 µm absolute filter remained below 0.15 MPa over an 8 h coating run when dissolution temperature was held below 40 °C; excursions above that threshold doubled the pressure rise and forced filter changeover, indicating microgel build-up.
The product differs from styrene-acrylic and polyester toner binders in four measurable respects: alcohol solubility, hydroxyl density, fusing rheology, and adhesion to corona-treated polyester. Styrene-acrylic binder systems typically require ester or aromatic co-solvents and offer residual hydroxyl content below 3 wt%; their solutions show lower viscosity at equal solids but weaker interaction with metal-azo charge-control agents. Low-molecular-weight polyester binders exhibit near-Newtonian melt flow between 120 °C and 160 °C, while PVB shows pronounced shear-thinning, reducing cold offset but narrowing hot offset latitude. Replacing a polyester binder with PVB at equal 50 wt% loading typically shifts minimum fixing temperature upward by 10–20 °C and raises melt viscosity at 150 °C by approximately 2–3× as measured by capillary rheometry at 100 s⁻¹.
| Parameter | PVB-RC 60 T | Styrene-acrylic toner binder | Low-molecular-weight polyester toner binder |
|---|---|---|---|
| Residual polar functionality | 18–21 wt% as PVOH | 0–3 wt% hydroxyl monomer | Acid value 10–30 mg KOH/g |
| Glass transition temperature | 68–72 °C | 55–65 °C | 55–65 °C |
| Solvent compatibility | Ethanol, methyl ethyl ketone, glycol ethers | Toluene, methyl ethyl ketone, esters | Methyl ethyl ketone, esters, limited alcohol solubility |
| Melt flow at 150 °C | Shear-thinning, higher viscosity | Moderate shear-thinning | Near-Newtonian, lower viscosity |
| Adhesion to corona-treated PET | Class 0–1 without primer | Requires primer or higher fusing energy | Requires higher fusing energy or primer |
| Moisture uptake at 50% RH | 1.0–1.5 wt% | 0.1–0.5 wt% | 0.3–0.8 wt% |
| Tribocharge versus ferrite carrier | Negative, 18–25 µC/g | Negative, tunable 10–40 µC/g | Negative, lower surface polar density |
Unlike architectural PVB grades for laminated glass, this reprographic grade is not plasticized. Interlayer-grade PVB typically requires 20–30 phr plasticizer to obtain melt-processable behaviour; that plasticizer level would suppress triboelectric charge and block resistance in dry toner. In diazo and vesicular reprographic coatings, the absence of plasticizer is necessary to maintain dimensional stability and to prevent migration of low-molecular-weight species into the photosensitive layer. Users switching from a general-purpose PVB grade should not assume equivalence because variations in residual hydroxyl content as small as 2 wt% alter solution filtration behaviour, carrier charge, and minimum fixing temperature. The product should be validated on the intended coating head and toner milling line before full substitution.