Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H19/00—Coated paper; Coating material
  • D21H19/80—Paper comprising more than one coating
  • D21H19/84—Paper comprising more than one coating on both sides of the substrate
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
  • D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
  • D21H17/74—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic and inorganic material
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H19/00—Coated paper; Coating material
  • D21H19/36—Coatings with pigments
  • D21H19/38—Coatings with pigments characterised by the pigments
  • D21H19/385—Oxides, hydroxides or carbonates
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H19/00—Coated paper; Coating material
  • D21H19/36—Coatings with pigments
  • D21H19/38—Coatings with pigments characterised by the pigments
  • D21H19/42—Coatings with pigments characterised by the pigments at least partly organic
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
  • D21H21/50—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by form
  • D21H21/52—Additives of definite length or shape

Definitions

• the present invention relates to paper coating pigments. More particularly, the present invention relates to a paper coating composition comprising plastic pigments and calcium carbonate, to methods for preparing the composition, to the use of the composition in paper coating, and to coated paper prepared with the said composition.
• paper means any kind of paper, but also board, card, paperboard and the like.
• Coated paper is used for a large range of products including packaging, art paper, brochures, magazines, catalogues and leaflets.
• Such paper is coated with an aqueous composition, known as a “coating composition” or sometimes as a “coating color”, so as to impart to said coated paper a number of properties, such as opacity, paper gloss, brightness, whiteness or printability, including print gloss.
• the coating compositions are generally made of water and of one or more inorganic pigments, such as kaolin, calcium carbonate, talc and/or titanium dioxide. They also comprise one or more binders, which may be of natural origin, such as starch, casein or carboxymethylcellulose (CMC), and/or of synthetic origin, such as the emulsions of latexes: styrene butadiene, styrene-acrylate copolymers or vinyl copolymers. Finally, they may include various additives such as, for example, dispersants, thickeners, water retention agents and/or optical brighteners.
• inorganic pigments such as kaolin, calcium carbonate, talc and/or titanium dioxide. They also comprise one or more binders, which may be of natural origin, such as starch, casein or carboxymethylcellulose (CMC), and/or of synthetic origin, such as the emulsions of latexes: styrene butadiene, styrene
• the productivity, quality and cost reduction goals greatly influence the composition of the coating composition, the number of layers and the coat weights.
• LWC light weight coated
• ULWC ultra light weight coated
• LLWC light lightweight coated
• Such types of paper are indeed produced at low cost, in large quantities, on high speed machines.
• the coat weights are very low. These materials may be coated once and are then called “single coated”. They me be coated twice with a pre-layer followed by a top layer and then they are called “double coated”.
• the coating composition may conveniently be applied by means of blade coaters, or by transfer rolls coaters called Metering Size Press or possibly by a curtain coater.
• LWC paper is defined as coated to a coating weight of from about 5 g/m 2 to about 13 g/m 2 on each side, for a total grammage (weight per unit area of the coated paper) in the range of from about 49 g/m 2 to about 65 g/m 2 .
• ULWC paper is defined as coated to a coating weight from 5 g/m 2 to 7 g/m 2 per side, for a grammage in the range of from about 35 g/m 2 to about 48 g/m 2 .
• Clay or equivalently referred to as kaolin hereafter, is generally used for preparing coating compositions for the manufacture of LWC and ULWC paper.
• Kaolin clay presents the advantage of providing paper gloss and print gloss.
• kaolin in paper coating composition has one major drawback: an increase of the coating composition solids content generates very high viscosities under high shear rates, which then leads to too high pressure of the metering devices of the coating machines or uncontrolled coat weights or the formation of coating defects such as splitting, bleeding or streaks.
• high shear rate viscosity i.e. viscosity ACAV at 10 6 s -1
• the greater the high shear rate viscosity the greater the blade pressure must be to control the deposited coat weight.
• a simple solution to the technical problem of excessive blade pressure would be to reduce the solids content of the coating composition by diluting the dry extract to reduce viscosity.
• the energy required for then drying the wet layer would be increased and the quality of the coated paper would be significantly affected.
• An object of the present invention is thus to provide an alternative to the use of kaolin in pigment compositions of paper coating colors.
• Another object of the present invention is to provide a solution to the problem of high viscosity under high shear rate associated with the use of kaolin in paper coating compositions.
• the specific combination of calcium carbonate particles with hollow sphere latex pigments, used as pigment composition in paper coating composition allow a significant reduction of composition viscosities under high shear rates, and then allow to increase the solids content of the coating composition while maintaining good operating conditions that remain within the usual limits of adjustment.
• the inventors have been able to show that increasing the solids content of the paper coating composition also has the following advantages: first of all, reduction of energy consumption when drying the coated paper; gloss maintained due to increased solids content; and need for binders and additives (including optical brightener) reduced.
• the combination of calcium carbonate particles and hollow latex pigments used as pigment composition for paper coating allow to meet the conditions needed for the preparation of LWC and ULWC papers, viz. rheology of the paper coating composition adapted to coating processes and high solids content of the paper coating compositions.
• the coating composition according to the present invention comprises an aqueous suspension of the defined particulate pigment together with the binder and water, and optionally one or more further additive components, as discussed above.
• compositions according to the present invention preferably consist essentially of an aqueous suspension of the defined particulate pigment, the binder and water, and optionally one or more further additive selected from the list of additive types given above, with less than about 10% by weight of other ingredients.
• the paper coating composition according to the present invention comprises an aqueous suspension of pigments together with binder, wherein the pigment composition comprises, consists essentially of or consists of:
• the paper coating composition according to the present invention comprises an aqueous suspension of pigments together with binder, wherein the pigment composition consists essentially of:
• the paper coating composition is intended for use to coat paper or substrate at a coating weight of less than or equal to 13 g/m 2 per side, e.g. less than or equal to 12 g/m 2 or less than or equal to 11 g/m 2 .
• This coating rate corresponds to light weight coated (LWC) paper and ultra light weight coated (ULWC) paper, also known as light lightweight coated (LLWC) paper.
• paper coating composition is intended for use to coat paper or substrate at a coating weight ranging from 5 g/m 2 to 13 g/m 2 per side.
• paper coating composition is intended for use to coat paper or substrate at a coating weight of less than or equal to 11 g/m 2 per side.
• the paper coating composition of the invention more particularly allows a decrease of the viscosity of the coating at a high shear rate (ACAV viscosity), while maintaining the viscosity of the coating at low shear rate (Brookfield viscosity) as high as possible.
• This compromise corresponds to obtaining a paper coating that is both workable (maintaining the low gradient viscosity), and can be used for coating at high speed or with a high solids content (decreasing the high-gradient viscosity, to counterbalance the increase in blade pressure).
• This property is particularly advantageous in high-speed coating processes (1 000 to 2 000 m/s) or those implementing high solids-content coatings (greater than 70% of their total weight) or those characterized by a low deposit, or a combination of these processes. Additionally, these results may be obtained by substantially decreasing the quantities of additives (thickeners, optical brighteners, latex%) in the formulation: as a result, the cost of the formulation is greatly improved.
• High shear rate viscosity is a determining factor in which blade pressure to apply. The greater the high shear rate viscosity, the greater the blade pressure must be to control the deposited coat weight. It is thus important to decrease the high-gradient viscosity, to counterbalance the increase in blade pressure.
• the Applicant has been able to identify and demonstrate that the combination of calcium carbonate (mineral pigment) along with hollow latex pigments (plastic pigment, more precisely Celocor®) in a paper coating is what leads to such a result, even with substantially no kaolin in the composition.
• the pigment composition comprises, consists essentially of or consists of:
• the pigment composition comprises, consists essentially of or consists of:
• Pigment 1 void latex particles:
• the "void latex pigments”, or equivalently “hollow latex pigments”, of the present invention generally comprise a hollow interior and an outer shell which encloses the hollow interior, although as will be explained subsequently in more detail one or more additional layers may be present between the outer shell and the interior void of each particle.
• the void latex particles of the present invention may be characterized as being "non-film-forming.” By “non-film-forming” it is meant that the void latex particles will not form a film at ambient temperature or below, or in other words will only form a film at temperatures above ambient temperature. For the purposes of this specification, ambient temperature is taken as being in the range of 15°C to 45°C. Thus, for example, when incorporated into an aqueous coating composition, applied to a substrate temperature and dried or cured at ambient temperature or below, the void latex particles do not form a film.
• the void latex particles generally remain as discrete particles in the dried or cured coating.
• the void latex particles are capable of functioning as opacifiers; that is, when added in sufficient amount to a coating composition that would otherwise be transparent when dried, they render the dried coating composition opaque.
• opacifiers it is meant that the refractive index of a coating composition has a higher refractive index when the void latex particles of the present invention are present in a coating composition as compared to the same coating composition not including the void latex particles of the present invention wherein the refractive index is measured after the coatings are dry to the touch.
• outer shell polymer refers to the outer layer of the particle of the present invention after swelling.
• the void latex particles may have a diameter of at least 200 nm, at least 250 nm, at least 300 nm, at least 350 nm, or at least 400 nm and a diameter of not more than 700 nm, not more than 650 nm, not more than 600 nm, not more than 550 nm, or not more than 500 nm.
• the hollow interior generally has a diameter of at least 100 nm, at least 150 nm, or at least 200 nm, but typically is not more than 600 nm or not more than 500 nm or not more than 400 nm in diameter.
• the thickness of the layers surrounding the hollow interior, including the outer shell and also any additional layers which may be present, generally is from 40 to 120 nm.
• the void latex particles will be approximately spherical in shape, although oblong, oval, teardrop or other shapes are also possible.
• the outer shell is polymeric and may, for example, be comprised of a thermoplastic polymer.
• the outer shell polymer may have a glass transition temperature (Tg) above ambient temperature, typically at least 60°C, at least 70°C, at least 80°C or at least about 90°C.
• Tg glass transition temperature
• the Tg of the outer shell polymer may be, for example, from 60°C to 140°C.
• the void latex particles of the present invention may be prepared by different methods, including, for example, by processes which utilize multi-stage emulsion polymer particles.
• the multi-stage emulsion polymer particles may comprise a core comprising a polymer of at least one hydrophilic monoethylenically unsaturated monomer and an outer shell comprising an outer shell polymer including monoethylenically unsaturated monomer.
• the multi-stage emulsion polymer particles may be contacted with a swelling agent, such as a base, which is capable of swelling the core, particularly in the presence of water.
• the swollen core causes the outer shell to expand, such that when the polymer particles are subsequently dried and/or re-acidified the outer shell remains enlarged in volume and a void is created within the particle as a result of the shrinkage of the swollen core.
• the void latex particles may each contain a single void. However, in other embodiments of the invention, the individual void latex particles may contain a plurality of voids (e.g., a void latex particle may contain two or more voids within the particle).
• the voids may be connected to each other through pores or other passageways.
• the voids may be substantially spherical in shape, but may adopt other forms such as void channels, interpenetrating networks of void and polymer, or sponge-like structures.
• the aforementioned multi-stage emulsion polymer particles may be prepared by sequential emulsion polymerization, using a batch process where the product of one stage is used in the stage that follows.
• the product of the core stage may be used to prepare the product of the next stage, be it an outer shell or an intermediate encapsulating polymer stage.
• the shell stage is prepared from the product of the core stage or, when there are one or more encapsulating polymer stages, an intermediate encapsulating polymer stage.
• the weight ratio of the core to the outer shell may generally, for example, be in the range of from 1:5 to 1:20 (e.g., from 1:8 to 1:15).
• the amount of outer shell relative to the amount of core should generally be decreased; however, sufficient outer shell should be present such that the core is still encapsulated.
• the particle size of the dry void latex particles may be between 300 and 550 nm with a dry bulk density of between 0.55 to 0.70 g/cc.
• the heart of the void latex pigments is empty or filled with air.
• the percentage of hollow pigments can be determined by comparing the volume occupied by the latex pigments after having been compacted from a dilute solution in a centrifuge with the volume of non-empty in the same pigment dispersion composition.
• Pigment 2 calcium carbonate particles
• calcium carbonate particles refers to a material that comprises at least 80 wt.-% calcium carbonate, based on the total weight of the calcium carbonate particles.
• calcium carbonate in the meaning of the present invention comprises ground calcium carbonate (GCC) as well as precipitated calcium carbonate (PCC).
• GCC GCC in the meaning of the present invention is a calcium carbonate obtained from natural sources, such as limestone, marble, calcite or chalk, and processed through a wet and/or dry treatment such as grinding, screening and/or fractionating, for example by a cyclone or classifier.
• Precipitated calcium carbonate in the meaning of the present invention is a synthesized material, generally obtained by precipitation following a reaction of carbon dioxide and calcium hydroxide (hydrated lime) in an aqueous environment or by precipitation of a calcium- and a carbonate source in water. Additionally, precipitated calcium carbonate can also be the product of introducing calcium and carbonate salts, calcium chloride and sodium carbonate for example, in an aqueous environment.
• PCC may be vaterite, calcite or aragonite.
• the "particle size" of the calcium carbonate particles is described by its distribution of particle sizes.
• the value d x represents the diameter relative to which x % by weight of the particles have diameters less than d x .
• the d 20 value is the particle size at which 20 wt.-% of all particles are smaller
• the d 75 value is the particle size at which 75 wt.-% of all particles are smaller.
• the d 50 value is thus the weight median particle size, i.e. 50 wt.-% of all grains are bigger or smaller than this particle size.
• the particle size is specified as weight median particle size d 50 unless indicated otherwise.
• a Sedigraph 5120 device from the company Micromeritics, USA, can be used.
• the particles of calcium carbonate may be in slurry or suspension of CaCO 3 particles.
• slurry means a water suspension that comprises insoluble solids and optionally at least one additive.
• the particle size distribution of the calcium carbonate particles is such that at least 60% by weight of the particles have an equivalent spherical diameter of less than 2 ⁇ m, for example at least 70 wt. %, at least 80 wt. %, at least 90 wt. % of the particles have an equivalent spherical diameter of less than 2 ⁇ m
• the calcium carbonate particles have a weight median particle size d 50 from 0.1 to 100 ⁇ m, for example from 0.25 to 50 ⁇ m, from 0.3 to 5 ⁇ m, or from 0.4 to 3.0 ⁇ m.
• the binder of the composition according to the present invention may be selected from binders which are well known in the art.
• the binder may form from 4 wt. % to 30 wt. %, e.g. from 5 wt. % to 20 wt. %, especially from 5 wt. % to 15 wt. %, of the solids content of the composition (dry/dry).
• the amount employed will depend upon the composition and the type of binder, which may itself incorporate one or more ingredients.
• Suitable binders include starch, a styrene butadiene rubber latex, acrylic polymer latex, polyvinyl acetate latex, or styrene acrylic copolymer latex.
• binders and binder types may be used alone or in admixture with each other and/or with other binders, if desired.
• the solids content of the paper coating composition according to the present invention may be greater than about 63 wt. %, preferably at least about 65 wt. %, preferably as high as possible but still giving a suitably fluid composition which may be used in coating (e.g. up to about 75 wt.%).
• the coating composition has a solid content greater than 65% by weight, for example a solid content ranging from 65 wt. % and 72 wt. %.
• the coating composition according to the present invention may contain one or more optional additional components, if desired.
• Such additional components are suitably selected from known additives for paper coating compositions.
• the percentages by weight quoted are based on the dry weight of pigment (100%) present in the composition. Where the additive is present in a minimum amount the minimum amount may be about 0.01 % by weight based on the dry weight of pigment.
• Another aspect of the invention concerns a pigment blend for paper coating composition. More precisely, the present invention concerns a pigment composition to be used as the pigment component of the paper coating composition for preparing light weight coated paper (LWC) or a ultra light weight coated paper (ULWC).
• LWC light weight coated paper
• ULWC ultra light weight coated paper
• the pigment blend/composition of the invention comprises, consists essentially of or consists of:
• the pigment blend/composition of the invention comprises, consists essentially of or consists of:
• the pigment blend/composition of the invention comprises, consists essentially of or consists of:
• the pigment blend/composition of the invention comprises, consists essentially of or consists of:
• a method for preparing a coated paper comprising as a first step the application to the paper of a coating weight of less than or equal to 13 g/m 2 per side, of a coating composition comprising or consisting essentially of or consisting of:
• Another object of the invention consists of a method for decreasing high shear rate viscosity of a paper coating, wherein the coating comprises water, at least one binder, a pigment composition, and optionally a rheology-modifying agent and/or an optical brightener, wherein said pigment composition comprises, consists essentially of or consists of hollow latex pigments and calcium carbonate particles, with the proviso that the pigment composition does not contain kaolin.
• said paper coating is intended for use to coat paper or substrate at a coating weight of less than or equal to 13 g/m 2 per side, e.g. less than or equal to 12 g/m 2 or less than or equal to 11 g/m 2 .
• This coating rate corresponds to light weight coated (LWC) paper and ultra light weight coated (ULWC) paper, also known as light lightweight coated (LLWC) paper.
• the method is for decreasing high shear rate viscosity of a paper coating, and at the same time, maintaining the low shear rate viscosity of said paper coating.
• the method is for decreasing high shear rate viscosity of a paper coating having a solids content greater than about 63 wt. %, preferably at least about 65 wt. %, preferably as high as possible but still giving a suitably fluid composition which may be used in coating (e.g. up to about 75 wt. %).
• the method is for decreasing high shear rate viscosity of a paper coating having a solids content greater than about 65% by weight, for example a solid content ranging from 65 wt. % and 72 wt. %.
• the method is for decreasing high shear rate viscosity of a paper coating having a solids content greater than about 66% by weight, for example a solid content ranging from 66 wt. % and 72 wt. %.
• An aspect of the invention relates to the use of a pigment composition comprising hollow latex pigments and calcium carbonate particles, with the proviso that the pigment composition does not contain kaolin, for preparing a coating composition to be used at a coating weight of less than or equal to 13 g/m 2 per side.
• Another object of the invention relates to the use of a pigment composition comprising hollow latex pigments and calcium carbonate particles, with the proviso that the pigment composition does not contain kaolin, for decreasing high shear rate viscosity of a paper coating, wherein the coating comprises, consists essentially of or consists of water, at least one binder, said pigment composition, and optionally a rheology-modifying agent and/or an optical brightener.
• the methods of paper coating generally require a means of applying the coating composition to the material to be coated, viz. an applicator; and a means for ensuring that a correct level of coating composition is applied, viz. a metering device.
• coaters examples include air knife coaters, blade coaters, rod coaters, bar coaters, multi-head coaters, roll coaters, roll/blade coaters, cast coaters, laboratory coaters, gravure coaters, kiss coaters, liquid application systems, reverse roll coaters and extrusion coaters.
• the present invention also concerns a paper coated with a coating comprising a dry residue of the paper coating composition as described above.
• the paper is a light weight coated paper (LWC) or a ultra light weight coated paper (ULWC).
• LWC light weight coated paper
• ULWC ultra light weight coated paper
• This paper is intended for use for off-set printing process.
• Weight median grain diameter and grain diameter mass distribution of a particulate material were determined via the sedimentation method, i.e. an analysis of sedimentation behaviour in a gravimetric field.
• the measurement was made with a SedigraphTM 5120. The method and the instrument are known to the skilled person and are commonly used to determine grain size of fillers and pigments.
• the measurement was carried out in an aqueous solution of 0.1 % by weight of Na 4 P 2 O 7 .
• the samples were dispersed using a high speed stirrer and ultrasonic.
• Solids content (wt.-%) of a material in slurry wt.-%
• the weight solids content was determined using a Moisture Analyser MJ 33, Mettler Toledo.
• the Brookfield viscosity was measured after 1 minute of stirring by the use of a RVT model BrookfieldTM viscometer at a temperature of 20°C ( ⁇ 2°C), and a rotation speed of 100 rpm (revolutions per minute) with the appropriate disc spindle from N° 1 to 5.
• the ACAV viscosity was measured with a capillary rheometer (ACA®) at 25°C with the appropriate capillary.
• This example illustrates the preparation of paper coating compositions according to the present invention (INV) or outside of the invention (OI).
• Test #1 corresponds to the preparation of a coating composition outside of the invention, said composition comprising 40 parts of kaolin (Capim NP) and 60 parts of calcium carbonate (Hydrocarb® 90, Omya).
• the coating composition is formulated so as to present a solids content of 63 wt.-%.
• Test #2 corresponds to the preparation of a coating composition identical to the one of Test #1, except that the solids content has been increased to 67 wt.-%.
• Test #3 corresponds to the preparation of a coating composition identical to the one of Test #2 (solids content: 67 wt.-%.), except that the quantity of thickener (Rheocoat® 93) has been reduced by half.
• Test #4 illustrates the preparation of a coating composition according to the invention, said composition comprising 97 parts of calcium carbonate (Hydrocarb® 90, Omya) and 3 parts of hollow latex pigments sold by Arkema under the tradename Celocor®.
• the coating composition is formulated so as to present a solids content of 67 wt.-%.
• Test #5 illustrates the preparation of a coating composition according to the invention, said composition comprising 95 parts of kaolin and 5 parts of hollow latex pigments sold by Arkema under the tradename Celocor®.
• the coating composition is formulated so as to present a solids content of 66 wt.-%.
• the viscosity values, low shear rate and high shear rate, obtained for test #1 are compatible with the LWC and MWC paper application.
• the solids content of the composition is adjusted to 63 wt.-%, which has the major disadvantage of requiring more energy for drying paper.
• Test #2 Increasing the solids content of the composition leads to an increase of the viscosity at low shear rate, as well as at high shear rate, thereby rendering the composition inadapted to LWC paper coating process.
• Test #3 Reducing the amount of thickening in the coating composition does not solve the problem of high viscosity at high shear rate of test #2.
• Tests #4 and #5 The values of viscosity under high shear rate are all inferior to those of tests #2 and #3 at the same solids content (i.e. 66-67 wt.-%). These values of viscosity are compatible with the LWC coating processes.
• the coatings were also used to coat paper, simple application layer (11 g/m 2 ). Although the results are not shown in Table 1 above, the gloss level of the coated papers thus obtained with a coating according to the tests #4-5 is comparable to the one obtained with Test #1 and despite the absence of kaolin.
• hollow latex microspheres thus provides an alternative to the use of kaolin in paper coatings for LWC paper without compromising brightness, opacity or whiteness.

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• 2014
  • 2014-04-09 EP EP14305517.6A patent/EP2930266A1/fr not_active Withdrawn
• 2015
  • 2015-04-08 WO PCT/US2015/024815 patent/WO2015157357A1/fr active Application Filing

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