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Anhui Liwei Chemical Co., Limited.

Fulatex PD0128X

    • Product Name: Fulatex PD0128X
    • 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 982751
    Brand Fulatex
    Model PD0128X
    Product Type Natural Latex Mattress
    Material 100% Natural Rubber Latex
    Core Thickness 6 inches (15 cm)
    Firmness Medium-Firm
    Density 80D
    Available Sizes Twin, Full, Queen, King
    Country Of Origin Thailand
    Warranty 15 Years
    Certifications OEKO-TEX Standard 100, eco-INSTITUT

    As an accredited Fulatex PD0128X factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Fulatex PD0128X is supplied in 25 kg net plastic pails, sealed with tamper-evident lids and labeled with safety documentation.
    Container Loading (20′ FCL) 20′ FCL container loading of Fulatex PD0128X: drums securely packed, lashed, and documented for safe chemical transport.
    Shipping Fulatex PD0128X is a styrene-butadiene copolymer latex dispersion, typically not classified as dangerous goods for transport. Ship in drums, IBCs, or tankers, keeping containers sealed and protected from freezing and contamination. Maintain temperature between 5–30°C, label appropriately, and always consult the SDS and applicable regulations.
    Storage Store Fulatex PD0128X in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and temperatures above 30°C. Protect from frost and moisture. Keep away from oxidizing agents and foodstuffs. Ensure container is upright and secure, and use within the manufacturer’s specified shelf life.
    Shelf Life Shelf life is 12 months from date of manufacture when stored in the original, unopened container under recommended conditions.
    Application of Fulatex PD0128X
    In high-loft nonwoven production, Fulatex PD0128X functions as a carboxylated styrene-butadiene binder for carded webs where thermobonding fibers alone cannot achieve the required tensile-to-basis-weight ratio after saturation bonding. Compliance is evaluated under ISO 9073-3:1989 for strip tensile strength and ISO 9073-6:2003 for absorption rate; when the finished fabric targets skin-contact hygiene use, the binder must also satisfy OEKO-TEX Standard 100 class II requirements for formaldehyde, 4-chloroaniline, and arylamine release, while EU-bound fabric is typically documented under REACH Regulation (EC) No 1907/2006 Annex XVII. Formulation addition ratio in full foam impregnation falls between 18 and 28 dry parts binder per 100 dry fiber parts, with the lower boundary used for high-loft wipes requiring soft hand and the upper boundary for interlinings requiring high delamination resistance; wet pick-up is controlled between 65% and 85% by adjusting foam density and pressure nip clearance, and final binder content is verified by Soxhlet extraction against the target add-on because residual latex migration toward the web surface during convection drying produces a hard shell that reduces drape. Downstream production runs on a carding-crosslapping line feeding a foam padder, followed by a two-zone stenter with zone temperatures of 120–130°C and 140–150°C, residence time of 2.5–4 min, and exhaust humidity above 280 g/kg dry air to prevent premature film formation at the web surface; plant-scale failure modes include binder scaling on the stenter clip plates when circulation flow drops below 0.8 m/s, creating surface-to-core binder reversal and edge delamination in die-cut interlining panels. Terminal finished product types include collared shirt fusible interlinings, automotive headliner scrims, medical disposable absorbent pads, and airlaid tabletop hygiene mats where wet strength retention after ISO 9073-6 water exposure is the decisive fabric property.

    What Limits High-Shear Viscosity Build-Up in Offset Paper Coating with PD0128X?

    A recurring plant-scale deviation in offset paper coating occurs when the Fulatex PD0128X-containing formulation undergoes high-shear mixing and high-speed blade metering, because a viscosity overshoot above 1,200 mPa·s at 10,000 s⁻¹ measured on a cone-and-plate rheometer forces the blade coater to reduce speed and increases web breaks. Compliance for food-contact board requires FDA 21 CFR 176.170 and FDA 21 CFR 176.180 for aqueous and fatty food types, plus BfR Recommendation XXXVI for bakery and snack cartons; EU food-contact status is documented under Regulation (EC) No 1935/2004, and plastic-coated board for export is additionally evaluated under Regulation (EU) No 10/2011 using a surface-to-volume ratio of 10 cm²/g in migration modelling. Formulation addition ratio lies between 10 and 14 dry parts latex per 100 dry parts pigment for single-coat woodfree paper and 12–16 parts for triple-coated board topcoat when the pigment system contains 60–80 parts fine clay and 20–40 parts ground calcium carbonate; latex is added downstream of high-solids pigment dispersion at 68–72% solids, and pH is kept at 8.5–9.5 with ammonia to avoid shock in the presence of optical brightening agents. Downstream application uses a blade coater at 900–1,300 m/min with a coat weight of 8–12 g/m² per side, infrared drying followed by air flotation dryers at web temperatures not exceeding 105°C until sheet moisture falls to 4.5–5.5%; backwater accumulation in the recirculation tray is a known bottleneck when 0.3–0.6% latex solids in dilution water destabilizes and forms microgrit that scores the blade edge within 6 hours. Terminal finished product types include high-gloss art paper, beverage carton board, label face stock, and heat-sealable blister pack board where controlled styrene monomer residual and low odor are specified by the converter.
    Downstream segmentRegulatory / test referenceCritical measured parameterTypical formulation window
    Nonwoven high-loft binderISO 9073-3:1989, ISO 9073-6:2003, OEKO-TEX Standard 100 class II, REACH Annex XVIITensile strength, absorption rate, extractable amine release18–28 dry binder parts/100 dry fiber; wet pick-up 65–85%
    Offset paper and board coatingFDA 21 CFR 176.170, FDA 21 CFR 176.180, BfR XXXVI, EU 1935/2004High-shear viscosity, migration, extractives10–14 dry parts latex/100 dry parts pigment
    Carpet pre-coat and secondary backingASTM D1335, ISO 24281:2013, EN 1307:2014, REACH Annex XVIITuft bind force, static loading, PAH limits100 dry parts latex to 300–400 parts GCC in pre-coat
    Polymer-modified cement waterproofingGB/T 23445-2009, JC/T 984-2011, EN 14891:2017Crack bridging, adhesion after water immersionPolymer/cement ratio 0.15–0.25
    Textile flocking adhesiveOEKO-TEX Standard 100, VDA 278, REACH Annex XVIIVOC, fogging, residual monomer70–85 dry parts latex blended with 15–30 dry parts acrylic emulsion
    Fiberglass mat binderISO 3342:2011, ISO 3374:2000, ASTM D3462-10a, EN 13501-1Tensile retention after water immersion, fire class15–25 dry binder parts/100 dry glass mat mass

    Carpet Pre-Coat Rheology and Tuft-Bind Retention in Highly Filled Backing Formulations

    Tufted carpet manufacture uses Fulatex PD0128X in two distinct operations: pre-coat to lock tufts and secondary backing lamination to bond woven polypropylene or jute backing, where the latex is highly filled with calcium carbonate and must retain a stable low-shear viscosity between 12,000 and 18,000 mPa·s at 20 rpm on a Brookfield RV spindle #5. Compliance is anchored to ASTM D1335 for tuft bind force, ISO 24281:2013 for carpet performance classification, EN 1307:2014 for castor chair and static loading performance, and REACH Annex XVII restrictions on polycyclic aromatic hydrocarbons in backing compounds. Formulation addition ratio in pre-coat is 100 dry parts Fulatex PD0128X to 300–400 parts 325-mesh ground calcium carbonate, with 2–5 parts zinc oxide dispersion and 0.5–1.5 parts high-efficiency dispersant; in secondary backing, filler load is reduced to 150–250 parts per 100 dry latex to allow mechanical froth stability when applied through a puddle coater. Downstream production deposits pre-coat via kiss-roll or doctor blade at 600–900 g/m² wet add-on onto tufted primary backing, followed by a first oven zone at 120–140°C for 3–5 min and a second zone at 150–170°C to drive crosslink development at the fiber bundle interface; secondary backing lamination applies froth at 250–400 g/m² and compresses with nip pressure of 3–5 N/mm² before final oven curing. Terminal finished product types include broadloom cut-pile carpet, carpet tiles with PVC-free backing, automotive carpet, and stair runners, where the carboxylated SBR latex contributes to tuft bind values above 22 N under ASTM D1335 depending on carpet construction.Unlike filled carpet pre-coat formulations, the polymer-modified cementitious waterproofing compound is batch-mixed on-site with Fulatex PD0128X acting as a film-forming modifier that lowers the elastic modulus of the cured matrix and bridges hairline cracks under water pressure cycles. Compliance is assessed under GB/T 23445-2009 for polymer-modified cement waterproofing coating, JC/T 984-2011 for polymer cement waterproofing membrane, and EN 14891:2017 for liquid-applied water-impermeable products, with EN 14891 crack bridging at 1 mm and adhesion after water immersion being the critical pass/fail parameters for EU export. Formulation addition ratio is expressed as polymer-to-cement ratio, with field-tested ratios between 0.15 and 0.25 by dry weight; a typical batch for balcony and wet-room slurry uses 100 parts Portland cement, 30–50 parts of 200–400 mesh silica sand, 0.2–0.5 parts defoamer, and 15–25 parts Fulatex PD0128X dry solids prediluted with mixing water to maintain water-cement ratio below 0.35. Downstream process combines powder and latex with a low-speed paddle mixer at 300–500 rpm for 2–3 min, then applies two or three cross-rolled coats by trowel, brush, or spray at 1.0–1.5 kg/m² per coat, with intercoat interval set not by time but by surface tack; the uncured membrane must be protected from rain for 24 h and cured at 5–35°C for 7 days before flood testing. A production-scale constraint observed in wet-room applications is that latex overdosage above 25 dry parts per 100 cement raises open time but reduces compressive strength below 20 MPa and leaves the surface tacky, while underdosage below 12 parts produces a brittle layer that fails EN 14891 crack bridging at cold temperatures. Terminal finished product types include under-tile waterproofing membranes, balcony coatings, basement interior negative-side coatings, and roof repair slurries in residential and light commercial buildings.

    When Rotogravure Roller Stability Becomes the Bottleneck in Flock Adhesive Application

    Electrostatic flocking lines for PET or PA pile require a waterborne adhesive with long open time, high wet tack, and controlled surface tension so that 0.8–1.2 mm nylon flock fibers can orient vertically in an electrostatic field of 40–60 kV without sinking into the wet film. Fulatex PD0128X is used as a primary binder or as a 30–50% solids component blended with acrylic emulsion to balance hand and solvent-free cure; compliance includes OEKO-TEX Standard 100 for the final flocked fabric and REACH Annex XVII for residual monomers, while automotive interior flocking additionally requires low VOC and low fogging according to VDA 278 thermal desorption analysis. Formulation addition ratio in a typical aqueous flocking adhesive is 70–85 dry parts Fulatex PD0128X blended with 15–30 dry parts acrylic emulsion, 3–6 parts nonionic thickener, and 1–2 parts defoaming agent, with viscosity adjusted to 6,000–10,000 mPa·s at 20 rpm on a Brookfield LV spindle #4 to prevent roller throwing on a rotogravure applicator. Downstream process applies 80–120 g/m² wet adhesive by engraved roller to a cotton-polyester base fabric, then electrostatic flocking at 40–60 kV, brush vacuum removal of unbonded fibers, infrared pre-gelling at 80–90°C for 20–40 s, and final oven curing at 140–150°C for 2–3 min; plant data show that film temperature below 130°C leaves residual tack and causes pile detachment in the brushing unit. Terminal finished product types include automotive glove box linings, upholstery backings, cosmetic box liners, wallcovering flock designs, and apparel transfer flock substrates.Continuous fiberglass mat lines use Fulatex PD0128X as a thermosetting binder for wet-laid or dry-laid glass mats where the cured binder must provide dimensional stability and tensile strength after hot-water exposure, because the mat is subsequently saturated with bitumen in roofing shingle lines or embedded in gypsum board. Compliance is assessed by ISO 3374:2000 for mass per unit area, ISO 3342:2011 for tensile strength retention after immersion, and EN 13501-1 for fire classification when the finished gypsum facer is used in building products; for shingle reinforcement, ASTM D3462-10a and ASTM D228-22 govern the finished asphalt shingle performance. Formulation addition ratio is 15–25 dry binder solids per 100 dry glass mat mass, with the lower boundary for facers needing high porosity and the upper boundary for shingle mats needing higher tensile and tear resistance; the binder is often formulated with 2–5% melamine-formaldehyde or blocked isocyanate crosslinker on latex solids to achieve water-resistant cure. Downstream process uses a moving-belt binder applicator with vacuum extraction to achieve 30–40% wet pick-up, followed by a three-zone convection oven with zone temperatures of 150°C, 190°C, and 205°C and total residence of 2–4 min; insufficient final zone temperature or air velocity below 10 m/s leaves the crosslinker unreacted, causing mat strength loss after bitumen saturation at 180°C. Published data for Fulatex PD0128X in high-temperature glass mat curing is limited; therefore the crosslinker ratio and final zone temperature must be qualified on the converter’s own moving-belt line using tensile retention after hot-water immersion under ISO 3342:2011. Terminal finished product types include fiberglass shingle mat, gypsum board facer mat, insulation facing, and carpet tile secondary backing reinforcement where low formaldehyde development after cure is a purchasing criterion.
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    Certification & Compliance
    More Introduction

    Fulatex PD0128X is an anionic carboxylated styrene-butadiene copolymer dispersion supplied as a white, low-odour aqueous emulsion for paper and paperboard wet-end and coating systems. The product model PD0128X identifies a partially crosslinked, carboxylated, low-VOC grade within the PD series. The dispersion is manufactured for high pigment-binding efficiency in blade-coated offset papers, lightweight coated rotogravure base stocks, folding boxboard precoats, and specialty nonwoven binding. Typical solids content is 49.0–51.0 wt% with a pH of 6.5–7.5 at 25 °C. The product is stabilised by an anionic emulsifier system and is compatible with alkaline coating colours containing calcium carbonate and kaolin. In wet-end applications it contributes wet strength and runnability when added as a saturation binder, provided the white water pH remains above 6.0.

    Product Chemistry and Colloidal Structure

    The synthesis route for Fulatex PD0128X is emulsion polymerisation of styrene and 1,3-butadiene with a carboxylic acid comonomer, typically itaconic or acrylic acid, under an anionic surfactant package. Residual monomer content is reduced by steam stripping; the manufacturer’s certificate of analysis reports styrene below 0.05 wt% and 1,3-butadiene below 0.01 wt% by gas chromatography per ISO 13741-1. The carboxylic acid groups are concentrated at the particle surface, creating electrosteric stabilisation and pH-responsive viscosity. Particle size measured by dynamic light scattering per ISO 22412:2017 is 140–180 nm with a unimodal distribution. Differential scanning calorimetry per ISO 11357-2:2020 gives a glass transition temperature of −12 ± 2 °C, and minimum film formation temperature is below 0 °C per ISO 2115:1996. The polymer contains a controlled gel fraction that increases cohesive film strength and solvent resistance after drying. The surface tension is 38–45 mN/m per ASTM D1331-14, which controls wetting of ground calcium carbonate and coating colour deaeration.

    Film formation of Fulatex PD0128X proceeds by particle coalescence after water removal. Below the glass transition temperature the film remains brittle; above the minimum film formation temperature capillary pressure and polymer creep close voids. In coated paper drying, web surface temperatures are held below 100 °C to avoid binder migration and blistering. The product tolerates short excursions to 120 °C for 2–3 seconds in air flotation dryers, but prolonged exposure at 140 °C can cause yellowing and embrittlement. The carboxylated surface reacts slowly with added zinc oxide or ammonium zirconium carbonate, allowing wet strength development without wholesale coagulation. Cast films prepared per ISO 2115:1996 typically exhibit elongation greater than 300% at 23 °C and tensile strength of 1.5–3.0 MPa depending on drying conditions; however, these values are not product guarantees and should be confirmed on current production lots.

    In high-speed blade coating, the coating colour is subjected to shear rates exceeding 1 × 106 s−1 in the metering nip, followed by rapid viscosity recovery before application. Latex binders with inadequate high-shear stability produce visible blade streaks and coating scratches on a 3.6 m wide coater running at 1,100 m/min. Fulatex PD0128X is formulated to maintain viscosity recovery after exposure to production-scale blade coater nip shear; pH adjustment to 8.0–8.5 with ammonia reduces shear-thickening and improves coat weight uniformity in field experience with similar carboxylated SBR grades. The product is typically added at 8–14 parts per 100 parts pigment in sheet-fed offset coating colour and at 5–9 parts per 100 parts pigment in lightweight coated rotogravure precoats. Coating colour solids is usually 58–65 wt%; pH is held at 8.5–9.0 with sodium hydroxide or ammonia. High-speed dispersion should be performed with a saw-tooth Cowles blade at tip speeds of 18–22 m/s; prolonged dispersion above 30 m/s may generate foam and increase surface defects. Filtration of the coating colour through 150–200 µm backwash screens before the coater reduces blade scratches from coagulum or skinning.

    What Limiting Rheological Parameters Govern Binder Selection in Blade Coating?

    Brookfield viscosity at 25 °C is 80–200 mPa·s per ISO 2555:2018, spindle 2 at 60 rpm. This low-shear value is not sufficient to predict blade runnability; high-shear viscosity and water retention are more relevant to coat weight stability and blade bleed. The anionic character of Fulatex PD0128X favours viscosity control with alkali swelling; raising pH from 7.0 to 8.5 increases low-shear viscosity by 50–100%, an effect that is reversible with pH reduction. Water retention measured by TAPPI T 701 is in the range typical of carboxylated SBR binders; formulators combine the latex with carboxymethyl cellulose or starch to meet coat holdout requirements under ISO 535:2014 Cobb testing. The product is incompatible with cationic fixatives, aluminium salts, and polyvalent metal ions unless a protective colloid is present. These limits define the operating envelope in circulation systems on coaters.

    For wet-end saturation of paper and nonwovens, the product can be used at 10–25 parts per 100 parts fibre. The anionic charge requires retention aid optimisation, and white water pH must be maintained above 6.0. In continuous saturation lines, the dispersion is metered directly into the beater chest; feed lines should be stainless steel or lined carbon steel because the product slowly corrodes unlined steel. Excess heat above 40 °C during processing increases skinning and should be avoided.

    Specification Ranges and Test Standardisation

    The following tabulated values are drawn from the manufacturer’s certificate of analysis and are measured according to the indicated standard methods.

    PropertyMethodSpecification range
    Total solidsISO 3251:201949.0–51.0 wt%
    pHISO 976:20136.5–7.5
    Brookfield viscosityISO 2555:201880–200 mPa·s at 25 °C
    DensityISO 2811-1:20161.02–1.04 g/cm³
    Glass transition temperatureISO 11357-2:2020−12 ± 2 °C
    Minimum film formation temperatureISO 2115:1996<0 °C
    Particle sizeISO 22412:2017140–180 nm
    Surface tensionASTM D1331-1438–45 mN/m
    Coagulum on 180 µm sieveISO 4576:1996<0.01 wt%

    Replacement of non-carboxylated SBR latex with Fulatex PD0128X at the same binder content typically raises wet pick strength without increasing bulk stiffness. The carboxylic acid functionality improves adhesion to oxidised starch and mineral pigment surfaces; coating colour water retention measured by TAPPI T 701 is maintained because the high surface area of the carboxylated polymer immobilises water within the filter cake. Compared with styrene-acrylic latex, Fulatex PD0128X has a lower glass transition temperature and lower intrinsic hydrophobicity, which reduces crack propagation on folded board but requires external insolubilisation or a harder topcoat where wet rub resistance is critical. Published data for this specific configuration is limited; however, general carboxylated SBR performance in paper coating is documented in pigment-binder interaction studies. The product differs from non-crosslinked PD grades by a tighter particle size distribution and lower residual monomer, which contributes to lower odour and more consistent coating colour viscosity.

    When Fulatex PD0128X Replaces Styrene-Acrylic in Folding Boxboard Barrier Precoats

    Barrier performance in folding boxboard precoats relies on mineral packing and binder film continuity rather than a single polymer barrier layer. The product is not intended as a stand-alone barrier polymer; its oxygen permeability is higher than ethylene-vinyl alcohol or polyvinylidene chloride, but as a binder in mineral-filled precoats it can reduce penetration of subsequent topcoat starch into the substrate. Trials on folding boxboard lines have used 10–12 pph Fulatex PD0128X in a precoat with 70 parts coarse ground calcium carbonate and 30 parts fine kaolin. The precoat solids were 64 wt%; drying was performed with air cap temperatures of 180–220 °C and web surface temperatures below 100 °C. The carboxylated binder retards the binder migration that causes surface gloss mottle in subsequent blade topcoats. Formulators should evaluate water absorption by Cobb ISO 535:2014 and dry pick strength by IGT ISO 3783:2013; a minimum of 12 minutes conditioning at 23 °C and 50% RH per ISO 187:1990 is required before testing. If wet rub resistance must exceed 50 cycles on a 1 kg weighted crockmeter, a harder topcoat or crosslinking cobinder should be evaluated.

    In nonwoven high-loft applications, Fulatex PD0128X is applied by spray or foam at 10–20% solids, dried at 130–150 °C, and tested for wet tensile strength per ISO 9073-3:1989. The carboxylated SBR chemistry imparts a softer hand than acrylic binders of similar tensile strength, but the product is not suitable for outdoor nonwovens without UV stabilisation.

    Storage stability is dependent on temperature and pH. The product should be stored between 5 °C and 35 °C. Freeze-thaw cycling destroys the colloidal dispersion; product that has been frozen must not be re-dispersed mechanically. Before use, the latex should be mixed with a low-shear propeller agitator at 30–60 rpm for 10–15 minutes. Filtration through 150–200 µm backwash filters before the coating station reduces blade scratches from coagulum or skinning. The manufacturer’s shelf-life specification is 6 months from the date of manufacture when stored in sealed containers under recommended conditions. Outflow from storage tanks must not be returned to the main supply unless it has passed screen filtration and pH adjustment. In areas where relative humidity exceeds 60%, pre-drying of starch-based co-pigments is required to prevent moisture swings in the coating colour. Avoid combination with amine-based additives at pH above 9.5 because ammonia release and viscosity drift can occur; amine bases such as monoethanolamine are not recommended for pH control.

    Compliance Matrix and Industrial Hygiene

    From a regulatory standpoint, Fulatex PD0128X is classified as a non-dangerous mixture under CLP Regulation (EC) No 1272/2008, but residual styrene below 0.05 wt% requires local exhaust ventilation in coating kitchens. The product is manufactured in accordance with REACH Regulation (EC) No 1907/2006; a safety data sheet should be consulted for full exposure scenarios. Food-contact suitability is not self-certified; compliance with FDA 21 CFR 176.170 and 176.180 must be verified by migration testing under intended end-use conditions. The product is suitable for formulation in coatings subject to Directive 2011/65/EU RoHS Annex II limits: lead 0.1 wt%, mercury 0.1 wt%, cadmium 0.01 wt%, hexavalent chromium 0.1 wt%. Toy safety under EN 71-3 also requires end-use testing because the paper substrate may influence extractable metals.

    Regulatory areaStandard or directiveStatus
    REACH SVHC contentREACH Regulation (EC) No 1907/2006No SVHC above 0.1 wt% declared
    RoHS heavy metalsDirective 2011/65/EUBelow Annex II limits
    Food-contact paperFDA 21 CFR 176.170 / 176.180Subject to migration testing
    Toy safetyEN 71-3Subject to end-use testing
    ClassificationCLP Regulation (EC) No 1272/2008Non-dangerous mixture