+

WO2016004291A1 - Carbonates modifiés pour transport de poudre, stabilité de mélange à sec et charge de polymère améliorés - Google Patents

Carbonates modifiés pour transport de poudre, stabilité de mélange à sec et charge de polymère améliorés Download PDF

Info

Publication number
WO2016004291A1
WO2016004291A1 PCT/US2015/038964 US2015038964W WO2016004291A1 WO 2016004291 A1 WO2016004291 A1 WO 2016004291A1 US 2015038964 W US2015038964 W US 2015038964W WO 2016004291 A1 WO2016004291 A1 WO 2016004291A1
Authority
WO
WIPO (PCT)
Prior art keywords
acid
earth metal
alkali earth
metal carbonate
treated
Prior art date
Application number
PCT/US2015/038964
Other languages
English (en)
Inventor
Douglas Wicks
David ANSTINE
Christopher Paynter
David Taylor
Eric ERNST
Steven Dunn
Original Assignee
Imerys Pigments, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Imerys Pigments, Inc. filed Critical Imerys Pigments, Inc.
Publication of WO2016004291A1 publication Critical patent/WO2016004291A1/fr

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/02Compounds of alkaline earth metals or magnesium
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/02Compounds of alkaline earth metals or magnesium
    • C09C1/021Calcium carbonates

Definitions

  • compositions for use in transporting and processing functional fillers for use with polymeric resins such as vinyl chloride-based polymeric resins.
  • Polymeric resins may be used in melt processing, in which the polymeric resin is melted down and processed to form, for example, molded articles, monofilament fibers, or polymer films.
  • Commercial products can also be formed from polymeric films, such as for packaging or protective layers.
  • polymeric-based products may be used to make staple fibers, yarns, fishing line, woven fabrics, non-woven fabrics, artificial furs, diapers, feminine hygiene products, adult incontinence products, artificial turf, packaging materials, wipes, towels, industrial garments, medical drapes, medical gowns, foot covers, sterilization wraps, table cloths, paint brushes, napkins, trash bags, various personal care articles, pipes, gloves, automotive parts, toys, fasteners, and many other household, industrial, or commercial products.
  • thermoplastic polymeric resin which may incorporate various mineral fillers, such as calcium carbonate, during production of fibrous products, polymeric films, and molded parts.
  • mineral fillers such as calcium carbonate
  • increasing polymeric resin prices have created cost- benefits associated with increasing the quantity of mineral fillers and decreasing the quantity of resin in many products.
  • the required amount of virgin polymer resin material decreases while the end product may have comparable quality in areas such as strength, texture, and appearance.
  • Calcium carbonate is a commonly used filler/extender for the polymer industry.
  • a filler material may not include a surface treatment when processing certain polymers, such as vinyl chloride-based polymers.
  • filler compositions may clump or agglomerate due to moisture pick-up by the calcium carbonate.
  • the carbonate filler Prior to the processing, the carbonate filler may be transported in dry form.
  • the carbonate particles may be susceptible to moisture pick-up, which may cause the particles to stick together. Additional moisture may also cause clumps to form in the fillers.
  • the filler may also be susceptible to processing problems caused by friction as the carbonate passes through the delivery pipes during processing. The moisture pick-up susceptibility, clump formation, and reduction of static charges may create processing disruptions, which can reduce or negate the cost savings of using an untreated filler composition.
  • too little filler may be added to a polymeric resin if a blockage inhibits the flow of the filler in the processing equipment or too much filler may be added if the filler forms clumps that pass into the polymer or if a blockage breaks down and passes info the polymeric resin.
  • the blockage may be a large agglomerate that disrupts the processing, texture, or smoothness of the finished polymer. The output of a compounding line may also be reduced because machine operators must shut down the line to clear blockages and restore proper flow.
  • filler composition that reduces clumping and/or processing problems of the filler composition. It may also be desirable to provide a filler composition with improved handling and transportation characteristics with improved stability. It may also be desirable to provide a method for processing a polymeric resin, such that the flow properties of the filler are improved.
  • a blended functional filler composition for use with a vinyl chloride-based polymeric resin may include a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate.
  • a surface treatment of the treated alkali earth metal carbonate may include at least a monolayer concentration of the surface treatment.
  • a blended functional filler composition for use with a vinyl chloride-based polymeric resin may include a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate. The first treated alkali earth metal carbonate may have a surface treatment that may include at least a monolayer concentration of the surface treatment, and the second treated alkali earth metal carbonate may have a surface treatment that may include less than a monolayer concentration of the surface treatment.
  • a method of forming a filled vinyl chloride- based polymer article may include mixing a vinyl chloride-based polymeric resin with a filler composition, the filler composition including a blend of a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate, and forming a polymer article from the mixture.
  • a surface treatment of the treated alkali earth metal carbonate may include at least a monolayer concentration of the surface treatment.
  • a method of forming a filled vinyl chloride- based polymer article may include mixing a vinyl chloride-based polymeric resin with a filler composition, the filler composition including a blend of a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate, and forming a polymer article from the mixture.
  • the first treated alkali earth metal carbonate may have a surface treatment that may include at least a monolayer concentration of the surface treatment
  • the second treated alkali earth metal carbonate may have a surface treatment that may include less than a monolayer concentration of the surface treatment.
  • a blended functional filler composition for use with a vinyl chloride-based polymeric resin may include a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate.
  • a surface treatment of the treated alkali earth metal carbonate may include at least a monolayer concentration of the surface treatment.
  • a surface treatment of the treated alkali earth metal carbonate may include less than a monolayer concentration of the surface treatment.
  • a blended functional filler composition for use with a vinyl chloride-based polymeric resin may include a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate.
  • the first treated alkali earth metal carbonate may have a surface treatment that may include at least a monolayer concentration of the surface treatment
  • the second treated alkali earth metal carbonate may have a surface treatment that may include less than a monolayer concentration of the surface treatment.
  • a surface treatment of the first treated alkali earth metal carbonate may be different from a surface treatment of the second alkali earth metal carbonate.
  • a method of forming a filled vinyl chloride-based polymer article may include mixing a vinyl chloride-based polymeric resin with a filler composition, the filler composition including a blend of a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate, and forming a polymer article from the mixture.
  • a surface treatment of the treated alkali earth metal carbonate may include at least a monolayer concentration of the surface treatment.
  • Forming the polymer article from the mixture may include extruding the mixture to form the polymer article.
  • a method of forming a filled vinyl chloride-based polymer article may include mixing a vinyl chloride-based polymeric resin with a filler composition, the filler composition including a blend of a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate, and forming a polymer article from the mixture.
  • the first treated alkali earth metal carbonate may have a surface treatment that may include at least a monolayer concentration of the surface treatment
  • the second treated alkali earth metal carbonate may have a surface treatment that may include less than a monolayer concentration of the surface treatment.
  • a blended functional filler composition may be mixed with a vinyl chloride-based polymeric resin to form a polymer-filler blend.
  • the polymeric resin may include a polymeric resin powder.
  • a blend of the blended functional filler composition and a polymeric resin powder may stabilize the polymeric resin powder.
  • a blend of the blended functional filler composition and a polymeric resin powder may prevent clumping of the polymeric resin powder.
  • a blend of the blended functional filler composition and a polymeric resin powder may suitable for transport.
  • a filler material may include an alkali earth metal carbonate.
  • the alkali earth metal carbonate may include a carbonate of calcium, magnesium, barium, or strontium, or a carbonate of two or more alkaline earth metals, e.g., obtained from dolomite.
  • certain embodiments may tend to be discussed in terms of calcium carbonate, and/or in relation to aspects where the calcium carbonate is processed and/or treated. The invention should not be construed as being limited to such embodiments and may be applicable to any alkali earth metal carbonate.
  • a calcium carbonate-containing material may be produced in a known way from marble, chalk, limestone, dolomite, calcite, aragonite, precipitated calcium carbonate (PCC), or ground calcium carbonate (GCC).
  • a magnesium carbonate may be produced from, for example, magnesite.
  • the alkali earth metal carbonate may also include a synthetic alkali earth metal carbonate, such as, for example, synthetic calcium carbonate produced as a precipitate by a reaction of calcium hydroxide and carbon dioxide in a known way.
  • the alkali earth metal carbonate may be a ground carbonate.
  • the ground carbonate may be prepared by attrition grinding.
  • Altrition grinding refers to a process of wearing down particle surfaces resulting from grinding and shearing stress between the moving grinding particles.
  • Attrition can be accomplished by rubbing particles together under pressure, such as by a gas flow.
  • the attrition grinding may be performed
  • alkali earth metal carbonate particles are ground only by other alkali earth metal carbonate particles of the same type (e.g., calcium carbonate being ground only by calcium carbonate).
  • the alkali earth metal carbonate may be ground by the addition of a grinding media other than calcium carbonate.
  • a grinding media can include ceramic particles (e.g., silica, alumina, zirconia, and aluminum silicate), plastic particles, or rubber particles.
  • the calcium carbonate is ground in a mill.
  • Exemplary mills include those described in U.S. Patent Nos. 5,238,193 and 6,634,224. As described in these patents, the mill may include a grinding chamber, a conduit for introducing the calcium carbonate into the grinding chamber, and an impeller that rotates in the grinding chamber, thereby agitating the calcium carbonate.
  • the calcium carbonate is dry ground, such as, for example, where the atmosphere in the mill is ambient air. In some embodiments, the calcium carbonate may be wet ground.
  • the ground calcium carbonate may be further subjected to an air sifter or hydrocyclone.
  • the air sifter or hydrocyclone can function to classify the ground calcium carbonate and remove a portion of residual particles greater than, for example, 10 microns.
  • the classification can be used to remove residual particles greater than 50 microns, greater than 40 microns, greater than 30 microns, greater than 20 microns, greater than 15 microns, or greater than 5 microns.
  • the ground calcium carbonate may be classified using a centrifuge, hydraulic classifier, or elutriator.
  • the ground calcium carbonate disclosed herein may be free of dispersant, such as a polyacrylate.
  • a dispersant may be present in a sufficient amount to prevent or effectively restrict floccuiation or agglomeration of the ground calcium carbonate to a desired extent, according to normal processing requirements.
  • the dispersant may be present, for example, in levels up to about 1 % by weight relative to the dry weight of the alkali earth metal carbonate.
  • dispersants include polyelectrolytes such as polyacrylates and copolymers containing polyacrylate species, including polyacrylate salts (e.g., sodium and aluminium optionally with a Group II metal salt), sodium hexametaphosphates, non-ionic polyol, polyphosphoric acid, condensed sodium phosphate, non-ionic surfactants, alkanolamine, and other reagents commonly used for this function.
  • polyacrylate salts e.g., sodium and aluminium optionally with a Group II metal salt
  • sodium hexametaphosphates e.g., sodium and aluminium optionally with a Group II metal salt
  • sodium hexametaphosphates e.g., sodium and aluminium optionally with a Group II metal salt
  • non-ionic polyol e.g., polyphosphoric acid
  • condensed sodium phosphate e.g., non-ionic surfactants
  • alkanolamine e.g., al
  • a dispersant may be selected from conventional dispersant materials commonly used in the processing and grinding of alkali earth metal carbonate, such as calcium carbonate. Such dispersants will be recognized by those skilled in this art. Dispersants are generally water-soluble salts capable of supplying anionic species, which in their effective amounts may adsorb on the surface of the alkali earth metal carbonate particles and thereby inhibit aggregation of the particles.
  • the unsolvated salts suitably include alkali metal cations, such as sodium. Solvation may in some cases be assisted by making the aqueous suspension slightly alkaline.
  • Suitable dispersants also include water soluble condensed phosphates, for example, polymetaphosphate salts (general form of the sodium salts: (NaP0 3 ) x ), such as tetrasodium metaphosphate or so-called "sodium hexametaphosphate” (Graham's salt); water-soluble salts of polysilicic acids; polyelectrolytes; salts of homopolymers or copolymers of acrylic acid or methacrylic acid; or salts of polymers of other derivatives of acrylic acid, suitably having a weight average molecular mass of less than about 20,000.
  • Sodium hexametaphosphate and sodium polyacrylate the latter suitably having a weight average molecular mass in the range of about 1 ,500 to about 10,000, are preferred.
  • the production of the ground calcium carbonate includes using a grinding aid, such as propylene glycol, or any grinding aid known to those skilled in the art.
  • a grinding aid such as propylene glycol, or any grinding aid known to those skilled in the art.
  • the alkali earth metal carbonate may be treated to include a treatment layer located on the surface of the alkali earth metal carbonate mineral.
  • a surface-treatment may include a fatty-acid coating.
  • a surface treatment may include, for example, a treatment with an organic carboxylic acid.
  • the organic carboxylic acid may have the following general structure:
  • R is a carbon-containing compound having from 8 to 40 carbon atoms, such as, for example, from 8 to 40 carbon atoms.
  • organic carboxylic acid may include an aliphatic carboxylic acid, such as, for example, caproic acid, 2-ethylhexanoic acid, caprylic acid, neodecanoic acid, capric acid, valeric acid, lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid, lignoceric acid, tall oil fatty acid, napthenic acid, montanic acid, coronaric acid, linoleic acid, linoienic acid, 4,7,10,13,16,19- docosahexaenoic acid, 5,8,1 1 , 14, 17-eicosapentaenoic acid, hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, isononanoic acid, or combinations thereof.
  • an aliphatic carboxylic acid such as, for example, caproic acid, 2-ethylhexanoic acid,
  • the aliphatic carboxylic acid may be a saturated or unsaturated aliphatic carboxylic acid
  • the aliphatic carboxylic acid may include a mixture of two or more aliphatic carboxylic acids, such as, for example, a mixture of two or more of caproic acid, 2-ethylhexanoic acid, caprylic acid, neodecanoic acid, capric acid, valeric acid, lauric acid, myrisfic acid, palmitic acid, stearic acid, behenic acid, lignoceric acid, tall oil fatty acid, napthenic acid, montanic acid, coronaric acid, linoleic acid, linoienic acid, 4,7,10,13,18,19-docosahexaenoic acid, 5, 8, 1 1 , 14, 17- eicosapentaenoic acid, hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, and isononanoic acid.
  • aliphatic carboxylic acids such as, for example,
  • the weight ratio of a mixed aliphatic carboxylic acid including two component acids may range from about 90:10 to about 10:90 by weight, from about 80:20 to about 20:80, from about 70:30 to about 30:70, or from about 60:40 to about 40:60 by weight.
  • the weight ratio of the component aliphatic carboxylic acids in an acid mixture may be about 50:50 by weight.
  • the aliphatic carboxylic acid may include one or more of a linear, branched, substituted, or non-substituted carboxylic acid.
  • the aliphatic carboxylic acid may be chosen from aliphatic monocarboxylic acids. Alternatively or additionally, the aliphatic carboxylic acid may be chosen from branched aliphatic monocarboxylic acids.
  • the surface treatment may include an aromatic carboxylic acid, such as, for example, alkylbenzoic acid, hydroxybenzoic acid, aminobenzoic acid, protocatechuic acid, or combinations thereof.
  • aromatic carboxylic acid such as, for example, alkylbenzoic acid, hydroxybenzoic acid, aminobenzoic acid, protocatechuic acid, or combinations thereof.
  • the surface treatment may include a Rosin acid, such as, for example, palustrinic acid, neoabietic acid, abietic acid, or levopimaric acid.
  • Rosin acid such as, for example, palustrinic acid, neoabietic acid, abietic acid, or levopimaric acid.
  • R may include one or more of a straight chain or branched alkyi, phenyl, substituted phenyl, C8-40 alkyi substituted with up to four OH groups, C6-40 alkyi, amido, maleimido, amino or acetyl substituted hydrocarbon radicals.
  • the surface treatment may include a combination of one or more of an aliphatic carboxylic acid, an aromatic carboxylic acid, or a Rosin acid.
  • the organic carboxylic acid may be a liquid at room temperature, such as, for example, an organic carboxylic acid having a viscosity of less than 500 mPa-s at 23 °C when measured in a DV 111 Ultra model Brookfield viscometer equipped with the disc spindle 3 at a rotation speed of 100 rpm and room temperature (23+1 °C).
  • the alkali earth metal carbonate may be treated by forming a treatment layer including at least one organic carboxylic acid and/or one or more reaction products of at least one organic carboxylic acid on the surface of the alkali earth metal carbonate filler resulting in a treated alkali earth metal carbonate filler,
  • the treated alkali earth metal carbonate may include a stearate treatment, such as, for example, ammonium stearate, calcium stearate, barium stearate, magnesium stearate, strontium stearate, zinc stearate, aluminum stearate, zirconium stearate, or cobalt stearate.
  • a stearate treatment such as, for example, ammonium stearate, calcium stearate, barium stearate, magnesium stearate, strontium stearate, zinc stearate, aluminum stearate, zirconium stearate, or cobalt stearate.
  • the treated alkali earth metal carbonate may include a salt of at least one of a valerate, stearate, laurate, palmitate, caprylate, neodecanoate, caproate, myristate, behenate, lignocerate, napthenate, montanate, coronarate, linoleate,
  • docosahexaenoate, eicosapentaenoate, hexanoate, heptanoate, octanoate, nonanoate is ' ononanoate, or mixtures thereof, such as. for example, ammonium, calcium, barium, magnesium, strontium, zinc, aluminum, zirconium, or cobalt forms of the
  • the surface treatment may include a blend of a carboxylic acid and a salt of a carboxylic acid.
  • the weight ratio of a mixed carboxylic acid and salt thereof may range from about 90:10 to about 10:90 by weight (acid:salt), from about 80:20 to about 20:80, from about 70:30 to about 30:70, or from about 60:40 to about 40:60 by weight
  • the weight ratio of carboxylic acid and salt in a mixture may be about 50:50 by weight (acid:salt).
  • the treated alkali earth metal carbonate filler may have a volatile onset temperature of greater than or equal to about 100 °C. According to some embodiments, the treated alkali earth metal carbonate filler may have a volatile onset temperature of greater than or equal to about 130 °C, greater than or equal to about 150 °C, greater than or equal to about 160 °C, greater than or equal to about 170 °C, greater than or equal to about 200 °C, greater than or equal to about 220 °C, greater than or equal to about 250 °C, greater than or equal to about 260 °C, such as, for example, greater than or equal to 270 °C, greater than or equal to 280 °C, greater than or equal to 290 °C, greater than or equal to 300 °C, greater than or equal to 310 °C, or greater than or equal to 320 °C.
  • polymer As used in this disclosure, the terms “polymer,” “resin,” “polymeric resin,” and derivations of these terms may be used interchangeably.
  • the polymeric resin may be a vinyl chloride-based polymeric resin chosen from conventional vinyl chloride-based polymeric resins that provide the properties desired for any particular yarn, woven product, non- woven product, film, mold, or other applications.
  • the vinyl chloride-based polymeric resin may be a thermoplastic polymer, including but not limited to polyvinyl chloride (PVC).
  • the vinyl chloride-based polymeric resin may include unplasticized polyvinyl chloride (uPVC).
  • the vinyl chloride-based polymeric resin may include a chlorinated polyvinyl chloride polymeric resin.
  • the vinyl chloride-based polymeric resin may include a co-polymer, in which one of the polymers is a vinyl chloride-based polymer.
  • the vinyl chloride-based polymeric resin may include a co- polymer of polyvinyl chloride and at least one of ethylene-vinyl acetate (EVA), chlorinated polyethylene (CPE), acrylonitrile butadiene styrene (ABS), methacrylate butadiene styrene (MBS), Acrylonitrile butadiene rubber (NBR), thermoplastic polyurethane (c, Thermoplastic polyester elastomers (TPEE), or acrylic resins.
  • EVA ethylene-vinyl acetate
  • CPE chlorinated polyethylene
  • ABS acrylonitrile butadiene styrene
  • MVS methacrylate butadiene styrene
  • NBR Acrylonitrile butadiene rubber
  • c thermoplastic polyurethane
  • alkali earth metal carbonate fillers such as, for example, calcium carbonate-containing mineral fillers
  • processing problems such as clumping and reduced static charge, that may result in buildups in processing equipment, creating blockages that affect the flow of filler to a polymer.
  • adverse effects resulting from clumping may be mitigated by blending the alkali earth metal carbonates, such as, for example, with a blend of a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate, or a blend of a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate.
  • a blend may act as a process aid for melt-processing polymers for the formation of polymer articles, such as, for example, polymer pipe (e.g., polyvinyl chloride (PVC) pipe) and other polymer articles.
  • PVC polyvinyl chloride
  • such blends may act as a process aid as defined by the Plastics Pipe Institute (PPI).
  • PPI Plastics Pipe Institute
  • the blend may be a pre-qualified ingredient exempted from stress-rupture testing for PVC pipe as defined by PPI Technical Reports TR-2 and TR-3.
  • the blend may be a process aid resulting in a PVC pipe having a hydrostatic design basis of 4,000 psi for water at 73°F (23°C) when evaluated according to ASTM D 2837, as defined by PPI Technical Reports TR-2 and TR-3.
  • the blends may improve the flow, reduce clumping, and/or improve dry-blend stability (e.g., reduce separation of the functional filler and polymer) of powder, pellets, and/or granules including a polymer and the blend, in other embodiments, the blends may have improved dispersion in the polymer melt and/or polymer article as compared to a filler comprising only an untreated alkali earth metal.
  • dry-blend stability e.g., reduce separation of the functional filler and polymer
  • the blends may have improved dispersion in the polymer melt and/or polymer article as compared to a filler comprising only an untreated alkali earth metal.
  • Improved flow and/or dispersion in the polymer may provide improved control of the polymer formulation and/or process (e.g., dosing of the functional filler), which may increase permissible loading levels and/or loading consistency, and/or may improve throughput of the processing, thereby achieving higher running rates.
  • the loading level of the blend in the polymer may be increased by at least 1 %, or at least 10%, as compared to the loading level of a filler including only an untreated alkali earth metal.
  • the blend may provide better wall control of polymer articles such as pipe ⁇ e.g., allowing more consistent wall thicknesses and/or production to tighter tolerances).
  • the blend may result in maintaining and/or improving impact strength of the finished polymer article.
  • an alkali earth metal carbonate filler composition may include a blend of a treated alkali earth metal carbonate and an untreated alkali earth metal carbonate.
  • an alkali earth metal carbonate filler composition may include a blend of a first treated alkali earth metal carbonate and a second treated alkali earth metal carbonate.
  • the blend of treated and untreated alkali earth metal carbonates, or a biend of a first treated and second treated alkali earth metai carbonate may be referred to herein as a "blended" composition or "blended filler" composition.
  • a treated alkali earth metal carbonate may be treated as described above, such as, for example, with stearic acid and/or stearate.
  • first and second treated alkali earth metal carbonates blend may also apply to a first and second treated alkali earth metal carbonates blend, for example, such that a second treated alkali earth metal carbonates may replace the untreated alkali earth metal carbonates, or be added to the blend in addition to the untreated alkali earth metal carbonate.
  • the first treated alkali earth metal carbonate may have a different treatment from the second treated alkali earth metal carbonate.
  • the first treated alkali earth metal carbonate may be treated with stearic acid and the second treated alkali earth metal carbonate may be treated with stearate.
  • the ratio of treated to untreated alkali earth metal carbonate (or first treated alkali earth metal carbonate to second treated alkali earth metal carbonate) in the blended filler composition may range from about 20:1 to about 1 :20 (freated:untreated) by weight.
  • the ratio of treated to untreated alkali earth metal carbonate may range from about from about 10:1 to about 1 :10 (treated: untreated) by weight, from about 5:1 to about 1 :5 (treated: untreated) by weight, from about 4:1 to about 1 :4 (treated:untreated) by weight, from about 3:1 to about 1 :3 (treated: untreated) by weight, or from about 2:1 to about 1 :2
  • the ratio of treated to untreated alkali earth metal carbonate (or first treated alkali earth metal carbonate to second treated alkali earth metal carbonate) may be about 1 :1 by weight.
  • the treated portion of the blended filler composition improves the dispersion of the filler particles.
  • the dispersion may be improved by mitigating moisture pickup in the blended composition, thereby preventing the particles from clumping or agglomerating.
  • the flow properties of the filler composition may be improved to mitigate or prevent blockages from forming in the processing equipment.
  • a treated alkali earth metal carbonate may be treated with a monolayer concentration of the surface treatment.
  • “Monolayer concentration,” as used herein, refers to an amount sufficient to form a monolayer on the surface of the alkali earth metal carbonate particles. Such values will be readily calculable to one skilled in the art based on, for example, the surface area of the alkali earth metal carbonate particles.
  • a treated alkali earth metal carbonate may be treated with less than a monolayer concentration of the surface treatment.
  • a treated alkali earth metal carbonate may be treated with in excess of a monolayer concentration of the surface treatment.
  • the alkali earth metal carbonate may be surface treated in a treatment vessel containing a water-dry atmosphere in which the surface treatment is in a liquid (e.g., droplet) and/or vapor form.
  • a liquid e.g., droplet
  • calcium carbonate may be treated by exposing the calcium carbonate to a carboxylic acid, such as stearic acid, vapor or liquid.
  • the amount of vapor or liquid in the reaction vessel may be controlled so as not to exceed a monolayer concentration of the surface treatment.
  • the mixture may be blended at a temperature sufficient for at least a portion of the carboxylic acid to react (e.g., sufficient for a majority of the carboxylic acid to react) with at least a portion of the calcium carbonate.
  • the mixture may be blended at a temperature sufficient such that at least a portion of the carboxylic acid may coat at least a portion of the calcium carbonate (e.g., the surface of the calcium carbonate).
  • the alkali earth metal carbonate may be treated by exposing the surface of the alkali earth metal carbonate to the surface treatment agent in the reaction vessel at a temperature at which surface treatment is in a fluid or vaporized state.
  • the temperature may be in the range from about 20 °C to about 300 °C, such as, for example, from about 25 °C to about 100 °C, from about 50 °C to about 150 °C, from about 100 °C to about 200 °C, or from about 100 C C to about 150 °C.
  • the temperature selected in the atmosphere of the treatment vessel may provide sufficient heat to ensure melting and good mobility of the molecules of the surface treatment agent, and therefore, good contacting of and reaction with the surface of the alkali earth metal carbonate particles.
  • a mixture of the alkali earth metal carbonate and carboxylic acid, such as stearic acid may be blended at a temperature high enough to melt the carboxylic acid.
  • the alkali earth metal carbonate may be blended at a temperature in the range from about 65 °C to about 200 °C.
  • the mixture may be blended at a temperature in the range from about 85 °C to about 150 °C, for example, at about 120 °C.
  • the mixture may be blended at a temperature in the range from about 85 °C to about 100 °C. In still other embodiments, the mixture may be blended at a temperature in the range from about 65 °C to about 90 °C. In further embodiments, the mixture may be blended at a temperature in the range from about 70 °C to about 90 °C.
  • Surface treating the alkali earth metal carbonate may be carried out in a heated vessel in which a rapid agitation or stirring motion is applied to the atmosphere during the reaction of the surface treatment and with the alkali earth metal carbonate, such that the surface treatment agent is well dispersed in the treatment atmosphere.
  • the agitation should not be sufficient to alter the surface area of the alkali earth metal carbonate because such an alteration may change the required surface treatment agent concentration to create, for example, a monolayer concentration.
  • the treatment vessel may include, for example, one or more rotating paddles, including a rotating shaft having laterally extending blades including one or more propellers to promote agitation and deagglomeration of the carbonate and contacting of the carbonate with the surface treatment agent.
  • a treated calcium carbonate may be prepared by combining (e.g., blending) the carbonate with stearic acid and water at room temperature in an amount greater than about 0.1 % by weight relative to the totai weight of the mixture (e.g., in the form of a cake-mix).
  • the mixture may be blended at a temperature sufficient for at least a portion of the stearic acid to react (e.g.. sufficient for a majority of the stearic acid to react) with at least a portion of the surface of the calcium carbonate.
  • the mixture may be blended at a temperature sufficient such that at least a portion of the stearic acid may coat the surface of the calcium carbonate in a monolayer concentration.
  • an alkali earth metal carbonate such as calcium carbonate
  • stearic acid or other carboxylic acid
  • water in an amount greater than about 1 % by weight relative to the total weight of the mixture (e.g., in the form of a cake-mix) to inhibit the formation of free stearic acid.
  • the mixture may be blended at a temperature sufficient for at least a portion of the stearic acid to react (e.g., sufficient for a majority of the acid to react, for example, with at least a portion of the calcium carbonate).
  • the mixture may be blended at a temperature sufficient such that at least a portion of the stearic acid may coat at least a portion of the calcium carbonate (e.g., the surface of the calcium carbonate).
  • the treated alkali earth metal carbonate may be blended with an untreated alkali earth metal carbonate to form a blended composition.
  • the treated and untreated alkali earth metal carbonates may be mixed (e.g.. blended) together to promote dispersion of the untreated alkali earth metal carbonate throughout the treated alkali earth metal carbonate.
  • the mixing of the treated and untreated alkali earth metal carbonates may occur at room temperature or at an elevated temperature.
  • the treated alkali earth metal carbonate may be blended with a second treated alkali earth metal carbonate to form a blended composition.
  • Particle sizes, and other particle size properties, of the treated and untreated alkali earth metal carbonate may be measured using a SEDIGRAPH 5100 instrument, as supplied by icromeritics Corporation.
  • the size of a given particle is expressed in terms of the diameter of a sphere of equivalent diameter, which sediments through the suspension, i.e., an equivalent spherical diameter or esd.
  • the particle size of the treated alkali earth metal carbonate is expressed in terms of the particle size prior to the surface treatment.
  • an alkali earth metal carbonate may be characterized by a mean particle size (d 50 ) value, defined as the size at which 50 percent of the calcium carbonate particles have a diameter less than or equal to the stated value.
  • a treated alkali earth metal carbonate may have a dgo in the range from about 0.1 micron to about 50 microns, such as, for example, in the range from about 0.1 micron to about 30 microns, from about 0.1 micron to about 20 microns, from about 0.1 micron to about 10 microns, from about 0.1 micron to about 5 microns, from about 0.1 micron to about 3 microns, from about 0.1 micron to about 2 microns, from about 0.1 micron to about 1 micron, from about 0.5 microns to about 2 microns, from about 1 micron to about 5 microns, from about 5 microns to about 20 microns, or from about 5 microns to about 10 microns.
  • an untreated alkali earth metal carbonate may be characterized by a mean particle size (d 50 ) value in the range from about 0,1 micron to about 50 microns, such as, for example, in the range from about 0.1 micron to about 30 microns, from about 0.1 micron to about 20 microns, from about 0.1 micron to about 10 microns, from about 0.1 micron to about 5 microns, from about 0.1 micron to about 3 microns, from about 0.1 micron to about 2 microns, from about 0.1 micron to about 1 micron, from about 0.5 microns to about 2 microns, from about 1 micron to about 5 microns, from about 5 microns to about 20 microns, or from about 5 microns to about 10 microns.
  • d 50 mean particle size
  • a treated alkali earth metal carbonate may be characterized by a top cut size (dge) value, defined as the size at which 98 percent of the calcium carbonate particles have a diameter less than or equal to the stated value.
  • the treated alkali earth metal carbonate may have a d 98 in the range from about 2 microns to about 100 microns, such as, for example, in the range from about 5 microns to about 50 microns, from about 2 microns to about 20 microns, or from about 5 microns to about 20 microns.
  • an untreated alkali earth metal carbonate may be characterized by a top cut size (d 98 ) value in the range from about 2 microns to about 100 microns, such as, for example, in the range from about 2 microns to about 100 microns, such as, for example, from about 5 microns to about 50 microns, from about 2 microns to about 20 microns, or from about 5 microns to about 20 microns,
  • the treated alkali earth metal carbonate and the untreated alkali earth metal carbonate may have the same, substantially the same, or similar particle size distributions. According to some embodiments, the treated alkali earth metal carbonate and the untreated alkali earth metal carbonate may have different particle size distributions. For example, the treated alkali earth metal carbonate may have a larger particle size distribution than the untreated alkali earth metal carbonate, such as, for example, a larger median or mean particle size and/or a broader overall size distribution.
  • the treated alkali earth metal carbonate may have a smaller particle size distribution that the untreated alkali earth metal carbonate, such as, for example, a smaller median or mean particle size and/or a narrower overall size distribution.
  • the blended filler material may have, for example, a bimodal or multimodal distribution of particle sizes.
  • the first treated alkali earth metal carbonate and the second treated alkali earth metal carbonate may have the same, substantially the same, or similar particle size distributions, such as, for example, bimodal particle size distributions.
  • the d 5 o particle size ratio of may be, for example, greater than or equal to about 2:1 (treated: untreated or first treated: second treates), greater than or equal to about 3:1 (treated: untreated), greater than or equal to about 4: 1 (treated: untreated), greater than or equal to about 5:1 (treated ".untreated), greater than or equal to about 6:1 (treated:untreated), or greater than or equal to about 7:1 (treated: untreated).
  • the d 50 particle size ratio of may be, for example, greater than or equal to about 2: 1 (untreated:treated), greater than or equal to about 3:1 (untreated:treated), greater than or equal to about 4:1
  • a blended filler composition may have a major component and a minor component.
  • the major component represents the greater weight percent of the blend and the minor component represents the lesser weight percent of the blend.
  • the minor component may have a smaller median particle size (d 5Q ) than the major component,
  • the weight ratio of the minor component may range from about 1 :20 to about 4:10 (minor: major) by weight, such as, for example, from about 1 :10 by weight to about 3:10 by weight, or from about 1.5:10 to about 2.5:10 (minonmajor) by weight.
  • the ratio of the coarse component of the bfend to the fine component of the blend may range from about 20:1 to about 1 :20 by weight (coarse:fine), such as, for example, from about 10:1 to about 1 :10 by weight, from about 8:1 to about 1 :1 by weight, from about 8:1 to about 4:1 by weight, from about 8:1 to about 6:1 by weight, from about 5:1 to about 1 :1 by weight, from about 4:1 to about 2:1 by weight, from about 2:1 to about 1 :2 by weight, from about 1 :2 to about 1 :4 by weight, from about 1 :1 to about 1 :5 by weight, from about 1 :4 to about 1 :8 by weight, from about 1 :6 to about 1 :8 by weight, or from about 1 :1 to about 1 :8 by weight
  • a treated alkali earth metal carbonate may be treated with an organic carboxylic acid or salt thereof, or a mixture of an organic carboxylic acid and salt of an organic carboxylic acid.
  • some or all of the stearic acid may be replaced by ammonium stearate, calcium stearate, barium stearate, magnesium stearate, strontium stearate, zinc stearate. aluminum stearate, zirconium stearate, or cobalt stearate.
  • salts may include, for example, calcium valerate, barium valerate, magnesium valerate, strontium valerate, zinc valerate, aluminum valerate, zirconium valerate, or cobalt valerate, which may replace some or all of valeric acid.
  • some or all of the organic carboxylic acid may be replaced with a salt of the organic carboxylic acid.
  • carbolxylic acid may be replaced by a salt of at least one of a valerate, stearate, laurate, palmitate, caprylate, neodecanoate, caproate, myristate, behenate, lignocerate, napthenate, montanate, coronarate, linoleate,
  • the ratio of acid to salt may range from about 5:95 to about 95:5 (acid:salt) by weight, from about 10:90 to about 90:10 by weight, from about 80:20 to about 20:80 by weight, from about 70:30 to about 30:70 by weight, from about 60:40 to about 40:60 by weight, or from about 45:55 to about 55:45 by weight.
  • all of the stearic acid (or other surface treatment) may be replaced by a salt, such as stearate, which may be used to create a monolayer concentration on the alkali earth metal carbonate.
  • the alkali earth metal carbonate may be further subjected to an air sifter or hydrocyclone.
  • the air sifter or hydrocyclone can function to classify the ground calcium carbonate and remove a portion of residual particles greater than 20 microns.
  • the classification can be used to remove residua! particles greater than 40 microns, greater than 30 microns, greater than 15 microns, greater than 10 microns, or greater than 5 microns.
  • the ground calcium carbonate may be classified using a centrifuge, hydraulic classifier, or elutriator.
  • a treated alkali earth metal carbonate may have some or all of an organic carboxylic acid replaced with a salt of the carboxylic acid, and may, in some embodiments, be optionally blended with an untreated alkali earth metal carbonate.
  • a blended composition of alkali earth metal carbonates may include a blend of GCC and PCC.
  • the blend may include a treated GCC and an untreated PCC, a treated GCC and a treated PCC, or an untreated GCC and a treated PCC.
  • the GCC may have a d 50 greater than the d 50 of the PCC.
  • the blended composition may have a d 50 ratio of greater than or equal to about 2:1 (GCC:PCC), greater than or equal to about 3:1 (GCC:PCC), greater than or equal to about 4:1 (GCCPCC), greater than or equal to about 5:1 (GCCPCC), greater than or equal to about 6:1 (GCCPCC), or greater than or equal to about 7:1 (GCC: PCC).
  • GCC:PCC 2:1
  • GCC:PCC 3:1
  • GCCPCC GCCPCC
  • GCCPCC GCCPCC
  • GCCPCC GCCPCC
  • PCC 7:1
  • the GCC may have a d 50 that is about the same as the d 50 of the PCC.
  • the blended alkali earth metal carbonates may have a particle packing so as to allow more filler to be included in the polymer product while maintaining or improving the impact strength and/or stiffness of the polymer product.
  • the blended alkali earth metal carbonates may include a treated GCC having a d 50 greater than the d 50 of a treated PCC in the blend.
  • the blended alkali earth metal carbonates may include an untreated GCC having a d 50 greater than the d 5 o of a treated PCC in the blend.
  • the blended alkali earth metal carbonates may include a treated GCC having a d 5 o greater than the d 50 of an untreated PCC in the blend,
  • the treated and/or blended alkali earth metal carbonates may be used as a filler for a polymer product, such as, for example, a filler for a polymer fiber, film, extruded, or molded article.
  • the alkali earth metal carbonate filler may be incorporated into the vinyl chloride-based polymeric resin using any method conventionally known in the art or hereafter discovered.
  • alkali earth metal carbonate may be added to the vinyl chloride-based polymeric resin during any step prior to extrusion, for example, during or prior to the heating step or as a "masterbatch" in which the polymeric resin and the filler are premixed and optionally formed into granulates or pellets, and melted or mixed with additional virgin polymeric resin before forming a polymer-based article.
  • the virgin polymeric resin may be the same or different from the vinyl chloride-based polymeric resin containing the filler.
  • the molten vinyl chloride-based polymer may then be continuously extruded through, for example, at least one spinneret to produce long filaments. Extrusion of the filled polymer from the spinnerets may be used to create, for example, a non-woven fabric. According to some embodiments, the molten vinyl chloride-based polymer may then be continuously extruded through a nozzle or dye to form polymeric articles, such as. for example, pipes, rods, honey-comb structures, or other articles having variously-shaped cross-sections. The extrusion rate may vary according to the desired application, and appropriate extrusion rates will be known to the skilled artisan.
  • a vinyl chloride-based polymeric film may be created from the molten, filled vinyl chloride-based polymer according to methods known in the art or hereinafter discovered.
  • melt compounding may also be used to extrude films, tubes, shapes, strips, and coatings onto other materials, injection molding, blow molding, or casting, and thermoforming and formation of tubes or pipes.
  • the melt compounding may, for example, be carried out in, for example, a suitable compounder or screw extruder.
  • a vinyl chloride-based polymer material to be compounded may suitably be in a granular or pelletized form. The temperature of the compounding and molding, shaping or extrusion processes will depend upon the thermoplastic material being processed and materials incorporated therein.
  • filled vinyl chloride-based polymer compositions may be produced according to any appropriate process or processes now known to the skilled artisan or hereafter discovered.
  • the filled vinyl chloride-based polymer may include a monofilament fiber.
  • monofilament fiber may include the production of a continuous monofilament fiber of at least one polymeric resin and at least one filler.
  • Exemplary techniques include, but are not limited to, melt spinning, dry spinning, wet spinning, spinbonding, or meltblowing processes.
  • Melt spinning may include an extrusion process to provide molten polymer mixtures to spinneret dies.
  • monofilament fibers may be produced by heating the polymeric resin to at ieast about its melting point as it passes through the spinneret dies.
  • Control fillers and blended filler samples were prepared from treated and untreated calcium carbonates.
  • Control 1 included untreated calcium carbonate having a median particle size (d 50 ) of 3 microns.
  • Control 2 included a treated calcium carbonate having a median particle size (d 5 o) of 1.1 microns and coated with a monolayer concentration of stearic acid.
  • Samples A-C were prepared by blending the carbonates used in control 1 and control 2 at various weight ratios.
  • Sample A included 5% by weight of the treated calcium carbonate used in control 2 and 95% by weight of the untreated calcium carbonate used in control 1.
  • Sample B included 10% by weight of the treated calcium carbonate used in control 2 and 90% by weight of the untreated calcium carbonate used in control 1 .
  • Sample C included 20% by weight of the treated calcium carbonate used in control 2 and 80% by weight of the untreated calcium carbonate used in control 1.
  • Table 1 The relative compositions of the control samples and samples A-C are shown below in Table 1.
  • samples A-C which are blends of treated and untreated calcium carbonate, generally have a lower moisture pickup than the untreated carbonate
  • Dispersion of each of control 1 and 2, and samples A-C was measured after each of the moisture treatments. To measure dispersion, the weight of each composition was measured. The powder was then subjected to a light blast of air to determine the dispersion. The weight of a dry, empty shallow tray was measured. The fray was then filled with one of control 1 or 2, or one of samples A-C. The filled fray was then weighed and placed in a sealed chamber. A light pulse of air, of about 40 psi, was applied for about 0.3 seconds. The tray was then removed from the chamber and powder adhering to the tray edges was removed. The tray was then reweighed and compared to the original weight.
  • Samples B and C show increased dispersion after 10 days in the humidity chamber, as shown by the positive value of dispersed materia! relative to 0 days. This increased dispersion is believed to be attributable to the decreased moisture pick-up as compared to the untreated control material. It is also believed that the blended composition prevents the formation of agglomerates. At 21 days, although the dispersion of samples A-C decreased relative to 0 days, the dispersion loss was less than both of controls 1 and 2.
  • the dispersion of samples A-C was between about 0.2 wt% and about 2.5 wt% less than the dispersion at 0 days, whereas the dispersion of both control samples at 21 days was more than 5 wt% less than at 0 days, showing improved dispersion relative to controls 1 and 2.
  • blended samples A ⁇ C have less clumping and agglomeration than the control samples.
  • the material removed during dispersion included agglomerated particles
  • samples A ⁇ C included mostly unagglomerated particles.
  • blended samples A-C improve the processing characteristics of carbonate fillers by preventing agglomeration and improving the dispersion after time in relatively humid environments, as compared to both treated and untreated filler compositions.
  • Control samples and blended filler samples were prepared for treated and untreated calcium carbonates.
  • Control 1 included untreated calcium carbonate, as described in Example 1.
  • Control 3 included a treated calcium carbonate having a median particle size (d 50 ) of 3 microns and coated with a monolayer concentration of stearic acid.
  • Samples D-F were prepared by blending the carbonates used in control 1 and control 3 at various weight ratios.
  • Sample D included 5% by weight of the treated calcium carbonate used in control 3 and 95% by weight of the untreated calcium carbonate used in control 1.
  • Sample E included 10% by weight of the treated calcium carbonate used in control 3 and 90% by weight of the untreated calcium carbonate used in control 1.
  • Sample F included 20% by weight of the treated calcium carbonate used in control 3 and 80% by weight of the untreated calcium carbonate used in control 1.
  • Table 4 The relative compositions of the control samples and samples D-F are shown below in Table 4. TABLE 4
  • samples D-F which are blends of treated and untreated calcium carbonate, generally have a lower moisture pickup than the untreated carbonate,
  • control sample 3 As shown in Table 6, for control sample 3, the dispersion decreased over time as shown by less weight of powder being lost at 10 days and 21 days after placement in the humidity chamber. Similarly, the dispersion of control 1 decreased at by more than 5 wt% after 10 days in the humidity chamber. Although the dispersion of control 1 appears to increase after 21 days in Table 6, the removed materia! contained significant amounts of agglomerated material. As a result, control 1 exhibits the problems previously discussed relative to untreated materials, in which these
  • Samples E and F show increased dispersion after 10 days and 21 days in the humidity chamber, as shown by the positive value of dispersed material relative to 0 days.
  • the dispersion of sample D a decreased over time relative to 0 days, the dispersion loss was less than both of controls 1 and 3.
  • the dispersion of sample D was between about 0.4 wt% less than the dispersion at 0 days, whereas the dispersion of control 3 at 21 days was about 1 wt% less than at 0 days.
  • control 1 which was dispersed with agglomerated particles
  • the dispersed particles of sample D showed reduced agglomeration relative to the control sample.
  • samples D ⁇ F show improved dispersion characteristics relative to samples A-C.
  • Control samples and blended filler samples were prepared for treated and untreated calcium carbonates.
  • Control 4 included untreated calcium carbonate having a median particle size (d 50 ) of 0.7 microns.
  • Control 5 included a treated calcium carbonate having a median particle size (d 50 ) of 0.7 microns and coated with a monolayer concentration of stearic acid.
  • Samples G-L were prepared by blending the carbonates used in control 1 , control 3, control 4, and control 5 at various weight ratios.
  • Sample G included 10% by weight of the treated calcium carbonate used in control 5 and 90% by weight of the untreated calcium carbonate used in control 1 .
  • Sample H included 20% by weight of the treated calcium carbonate used in control 5 and 80% by weight of the untreated calcium carbonate used in control 1.
  • Sample I included 80% by weight of the treated calcium carbonate used in control 5 and 20% by weight of the untreated calcium carbonate used in control 1.
  • Sample J included 20% by weight of the treated calcium carbonate used in control 5 and 80% by weight of the untreated calcium carbonate used in control 4.
  • Sample K included 80% by weight of the treated calcium carbonate used in control 5 and 20% by weight of the untreated calcium carbonate used in control 4.
  • Sample L included 80% by weight of the treated calcium carbonate used in control 3 and 20% by weight of the untreated calcium carbonate used in control 4. The relative compositions of the control samples and samples G-L are shown below in Table 7.
  • samples G-L which are blends of treated and untreated calcium carbonate, generally have a lower moisture pickup than both of controls 4 and 5. As compared with sample A-F, samples G-L generally have a higher moisture pick-up value.
  • samples G and !-L the dispersion increased for all samples after 21 days in the humidity chamber. Dispersion in samples G and I, in which the treated material has a smaller particle size than the untreated material, improved after 21 days as compared to 0 days. Samples J and K, the median particle sizes of the treated and untreated compositions are similar, also show improved dispersion after 21 days.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

L'invention concerne une composition de charge fonctionnelle mélangée, destinée à être utilisée avec une résine polymère à base de chlorure de vinyle pouvant comprendre un carbonate de métal alcalino-terreux traité et un carbonate de métal alcalino-terreux non traité. Un traitement de surface du carbonate de métal alcalino-terreux traité comprend au moins une concentration monocouche du traitement de surface. Un procédé de formation d'un article polymère à base de chlorure de vinyle chargé peut comprendre le mélange d'une résine polymère à base de chlorure de vinyle avec une composition de charge et la formation d'un article polymère à partir du mélange. La composition de charge peut comprendre un mélange d'un carbonate de métal alcalino-terreux traité et d'un carbonate de métal alcalino-terreux non traité.
PCT/US2015/038964 2014-07-02 2015-07-02 Carbonates modifiés pour transport de poudre, stabilité de mélange à sec et charge de polymère améliorés WO2016004291A1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201462020145P 2014-07-02 2014-07-02
US62/020,145 2014-07-02
US201462067288P 2014-10-22 2014-10-22
US62/067,288 2014-10-22

Publications (1)

Publication Number Publication Date
WO2016004291A1 true WO2016004291A1 (fr) 2016-01-07

Family

ID=55019993

Family Applications (2)

Application Number Title Priority Date Filing Date
PCT/US2015/038964 WO2016004291A1 (fr) 2014-07-02 2015-07-02 Carbonates modifiés pour transport de poudre, stabilité de mélange à sec et charge de polymère améliorés
PCT/US2015/039015 WO2016004325A1 (fr) 2014-07-02 2015-07-02 Mélanges de carbonate revêtu d'acide gras avec du carbonate non traité destiné à être utilisé dans le traitement en fusion de polymères chargés de carbonate

Family Applications After (1)

Application Number Title Priority Date Filing Date
PCT/US2015/039015 WO2016004325A1 (fr) 2014-07-02 2015-07-02 Mélanges de carbonate revêtu d'acide gras avec du carbonate non traité destiné à être utilisé dans le traitement en fusion de polymères chargés de carbonate

Country Status (1)

Country Link
WO (2) WO2016004291A1 (fr)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4722816A (en) * 1985-05-21 1988-02-02 Shin-Etsu Chemical Co., Ltd. Method for the preparation of shaped articles of a vinyl chloride-based resin having improved surface properties
US6342100B1 (en) * 1997-09-03 2002-01-29 Solvay Soda Deutschland Gmbh Bimolecular coated calcium carbonate and process of production thereof
US20070258877A1 (en) * 2004-01-23 2007-11-08 Solvay (Societe Anonyme) Surface-Treated Calcium Carbonate Particles
US20130217819A1 (en) * 2010-05-28 2013-08-22 Matthias Buri Treated mineral filler products, process for the preparation thereof and uses of same

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4560712A (en) * 1984-12-27 1985-12-24 Mobil Oil Company Polypropylene compositions containing bimodal calcium carbonate and a polysiloxane
US4889878A (en) * 1988-04-15 1989-12-26 Dow Corning Corporation Flowable joint sealant for concrete highway
JP5179740B2 (ja) * 2006-09-28 2013-04-10 白石工業株式会社 加硫活性成分処理炭酸カルシウム
JP5284631B2 (ja) * 2007-12-11 2013-09-11 モメンティブ・パフォーマンス・マテリアルズ・ジャパン合同会社 室温硬化性ポリオルガノシロキサン組成物

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4722816A (en) * 1985-05-21 1988-02-02 Shin-Etsu Chemical Co., Ltd. Method for the preparation of shaped articles of a vinyl chloride-based resin having improved surface properties
US6342100B1 (en) * 1997-09-03 2002-01-29 Solvay Soda Deutschland Gmbh Bimolecular coated calcium carbonate and process of production thereof
US20070258877A1 (en) * 2004-01-23 2007-11-08 Solvay (Societe Anonyme) Surface-Treated Calcium Carbonate Particles
US20130217819A1 (en) * 2010-05-28 2013-08-22 Matthias Buri Treated mineral filler products, process for the preparation thereof and uses of same

Also Published As

Publication number Publication date
WO2016004325A1 (fr) 2016-01-07

Similar Documents

Publication Publication Date Title
CA2799456C (fr) Procede de preparation de produits a base de charges minerales traitees en surface et leurs utilisations
CA2734817C (fr) Produits de charge minerale traitee, procede pour leur preparation et leurs utilisations
JP6255478B2 (ja) 増加した充填剤含量を有する複合ポリマー材料の製造方法
EP3066053B1 (fr) Procédé pour améliorer la distribution de taille de particules d'un matériau contenant du carbonate de calcium
TWI582046B (zh) 製備包含碳酸鈣之碎粒的方法
US11535522B2 (en) Inorganic material composition and utilities thereof
WO2016004291A1 (fr) Carbonates modifiés pour transport de poudre, stabilité de mélange à sec et charge de polymère améliorés
US20170233553A1 (en) Modified carbonates for improved powder transportation and dry-blend stability
WO2016064941A1 (fr) Carbonates modifiés permettant d'améliorer le transport d'une poudre et la stabilité du mélange sec
KR20210069043A (ko) 조대 표면 처리된 충전재 생성물의 제조 방법
EP4446283A1 (fr) Carbonate de calcium traité en surface et composition de résine le contenant
US20180187019A1 (en) Coated alkaline earth metal carbonates and their uses
EP3931265A1 (fr) Procédé de préparation d'un matériau à base de carbonate de calcium traité en surface
EP3710147A1 (fr) Procédés de préparation et compositions comprenant des carbonates de métaux alcalino-terreux traités en surface et non traités
CN113348214A (zh) 制备经表面处理的碳酸钙材料的方法
CN113366049A (zh) 为聚合物制品提供改善的uv稳定性的表面处理的填料材料产品

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15814260

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 15814260

Country of ref document: EP

Kind code of ref document: A1

点击 这是indexloc提供的php浏览器服务,不要输入任何密码和下载