Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09C—TREATMENT 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
  • C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
  • C09C1/40—Compounds of aluminium
  • C09C1/42—Clays
• • 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
  • D21H19/40—Coatings with pigments characterised by the pigments siliceous, e.g. clays
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/50—Agglomerated particles
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/51—Particles with a specific particle size distribution
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/51—Particles with a specific particle size distribution
  • C01P2004/52—Particles with a specific particle size distribution highly monodisperse size distribution
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
  • C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
  • C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/14—Pore volume
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/19—Oil-absorption capacity, e.g. DBP values
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/21—Attrition-index or crushing strength of granulates
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/80—Compositional purity
  • C01P2006/82—Compositional purity water content
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/90—Other properties not specified above

Definitions

• This invention relates generally to kaolin products, and more specifically relates to a structured kaolin pigment and methods of manufacture of same.
• the pigment is useful as a filler in proper products and enables preparation of paper coat ⁇ ing formulations which yield resultant coated paper products of surprisingly enhanced properties.
• Titanium dioxide which can be incorporated into the paper in the form of anatase or of rutile. Titanium dioxide, however, is among the most expensive materials which are so useable. Thus despite the effectiveness of such material as a filler, its use is limited and satisfactory replacements have been much sought after.
• calcined kaolins are generally prepared by calcining a crude " kaolin which may have been initially subjected to prior beneficiation steps in order to remove certain impurities, e.g. for the purpose. of improving brightness in the ultimate product.
• kaolin pigment parti ⁇ cularly valuable for use as a filler are also well-known. These include a low abrasion value, and high brightness and opacifying characte isitics.
• the low abrasion is significant in order to assure that the resultant paper product may be manufactured and processed using conventional machinery without damaging same.
• the brightness and opacifying characte istics are important in producing an acceptable paper sheet, one which incorporates whiteness, high opacity, good printabilit , and light weight.
• Both the brightness characte istics of the given kaolin and the opacifying properties of same when .incorporated as a filler in paper may be quantitatively related to a property of the filler identified as the "scattering coefficient S".
• the said parameter i.e. the scattering coefficient S of a given filler pigment, is a property well-known and extensively utilized in the paper technology art, and has been the subject of numerous technical papers and the like. The early exposition of such measurements was made by Kubelka and Munk, and is reported in 2. Tech Physik 12:539 (1931). Further citations to the applicable measurement techniques and detailed. definitions of- he said scattering coefficient are set forth at numerous places in the patent and technical literature. Reference may usefully be had in this connection, e.g. to U.S. patents Nos .
• the major portion of filler should be in the range of one micrometer.
• good light scatter cannot be achieved solely by using a kaolin having the said size char ⁇ acteristics: an essential further characteristic needed is that the kaolin be structured, i.e., formed from an assemblage of platelets interconnected or bonded to provide aggregates which include a network of the platelets.
• Aggregation can be of interest for additional reasons.
• many kaolin crude reserves are considerably finer than preferred by the paper industry; i.e., they have an unduly high proportion of particles with E.S.D.'s below 0.25 micro ⁇ meters.
• Typical Cretaceous kaolins e.g., include 25 to 30% by weight of particles below 0.25 micrometers; and typical Tertiary kaolins can include 50 to 60% by weight of particles below 0.25 micrometers E.S.D.
• the presence of such large quantities of very fine particles can have detrimental. effects- upon paper strength, and in other respects are undesired by the paper manufacturer. While the said extreme fines can be removed by various separation processes, such as high speed centrifuging, such removal is very expensive and entails high capital investment; this quite aside from the possible loss of high proportions of the input feed.
• a calcined kaolin pigment is disclosed and a method for manufacture of same.
• the said pigment consists of porous aggre ⁇ gates of kaolin platelets, and exhibits exceptionally ' high light scattering characteristics when incorporated as a filler in paper.
• This pigment which substantially corresponds to the commercially available product ALPHATEX* of the present assignee Anglo-American Clays Corporation (Atlanta, Georgia) , is prepared by first blunging and dispersing an appropriate crude kaolin to form an aqueous dispersion of same.
• the blunged and dispersed aqueous slurry is subjected to a particle size separation from which there is recovered a slurry of the clay, which includes a very fine particle size; e.g. substantially all particles can be smaller than 1 micrometer E.S.D.
• the slurry is dried to produce a relatively moisture-free clay, which is then thoroughly pul- verized to break up agglomerates.
• This material is then used as a feed to a calciner; such feed is calcined under carefully con ⁇ trolled conditions to typical temperatures of at least 900°C.
• the resulting product is cooled and pulverized to provide a pig ⁇ ment of the porous high light scattering aggregates of kaolin platelets as described.
• Calcined kaolins have also found use in paper coating applications. Reference may be had to the paper by Hollings- worth, Jones, and Bonney, "The Effect of Calcined Clays on the Printability of Coated Rotogravure and Offset Printing Papers", TAPPI Proceedings, pages 9-16, 1983 Coating Conference, discuss ⁇ ing the advantages of incorporating small quantities of calcined kaolins into conventional kaolin-based coating formulations. Brightness and opacity of the paper both increase with increased calcined kaolin content, as may be expected from a pigment with high light scatter, and in some formulations gloss may show a slight increase with increasing calcined kaolin content.
• Calcined kaolin products including those of the afore ⁇ mentioned ALPHATEX® type, are seen to be manufactured by rela- tively complex techniques involving a multiplicity of steps, including specifically a calcining step, plus various preparatory steps and post-calcining steps.
• the said product is rela ⁇ tively expensive to produce; and requires considerable investment in complex apparatus and the like — e.g. highly regulated cal- ciners etc.
• the conditions of pre ⁇ paration of these materials must be very carefully controlled in order to keep abrasion acceptably low in the calcined product. For example the calcination operation tends per se to produce an abrasive product — in consequence of overheating -- if great care is not taken to preclude such a result.
• uncalcined sometimes referred to as "hydrous" kaolin both as paper fil ⁇ lers and for paper coating. Because the uncalcined material usually does not possess high light scattering qualities or good opacity, its usefulness, especially as a filler, is limited; and this (in addition to improving brightness) is indeed the parti ⁇ cular advantage of calcined products of the ALPHATEX type; i.e. by virtue of the aggregated structures of same, high light scattering properties are provided and good opacity.
• kaolinite is an aluminum hydroxide sili ⁇ cate of approximate composition AI2 (OH) 4Si2 ⁇ 5 (which equates to the hydrated formula just cited) .
• a composite silicate pig- ment prepared by a precipitation reaction where spherical hydrous metal silicate particles are precipitated on the planar surfaces of clay particles having a platelet-type structure.
• the metal silicate pigment component is comprised of the reaction product of a water soluble alkali metal silicate such as sodium silicate and a water soluble salt of a polyvalent metal, such as calcium chloride.
• pigmentary compositions are disclosed wherein comminuted minerals such as kaolins are combined with inorganic binders, and formed into agglomerates, which when calcined produce compositions embodying numerous particles of the minerals bonded together and presenting in ⁇ ternal voids and multiple light reflecting surfaces.
• the re- suiting pigmentary compositions are useful in applications re ⁇ quiring high visible light reflectance.
• a structured kaolin pigment product which possesses improved light scatter ⁇ ing characte istics, and hence is useful as an opacifier and light scattering filler for paper and paper products, and which may similarly be used in other paper manufacturing ' applications, including in the coating of same.
• lt is a yet further object of the invention, to pro ⁇ vide a process for producing a pigmentary high light scattering kaolin product, which process utilizes chemical aggregation techniques, and may be carried out without the use of a calcin- ing step or of other high temperature processing conditions or equipment.
• a still further object of the invention is to provide a process for producing structured kaolin pigments as aforemen- tioned, from a feed crude containing high percentages of extremely minute particles, e.g., less than 0.25 micrometers, to thereby convert a crude having limited value to the paper maker to one which can be readily and economically used in paper products.
• a yet further object of the invention is to provide a process as aforementioned, which enables low abrasion struc ⁇ tured kaolin pigments to be produced from coarser process feeds than can normally be employed in calcination to produce a product of comparable low abrasion. It is a further object of the invention to provide bulky structured kaolin pigments which are eminently suitable for paper coating applications.
• a yet further object of the invention is to provide improved papers of the type provided with a coating composition comprising a kaolin pigment and an adhesive binder, which papers, when manufactured pursuant to the invention, have improved opti ⁇ cal and printability properties over a very wide range of coating weights.
• a still further object of the invention is to provide improved paper and paperboard coating compositions, which so enhance coverage in relation to coating weight, as measured by gloss and other optical properties in resultant coated papers, as to enable a significant reduction in the coating weight, while yet maintaining the coverage, i.e. the gloss and other optical properties.
• a fine particle size kaolin feed is reacted in particulate form with a metal chloride, such as silicon tetrachloride, to form a chemically aggregated structured kaolin pigment.
• a metal chloride such as silicon tetrachloride
• Free moisture present in the particulate feed is sufficient to hydrolyze the metal chloride, but below levels at which the metal oxide will precipitate.
• a free moisture level of from about 0.4% to 1.0% by weight of the feed is preferred.
• the indicated steps are con ⁇ ducted under condi-tions such that the kaolinite structure is not impaired. Heating may optionally be used to shorten the reaction time. When so used, temperatures generally will not, however, exceed about 150°C.
• the kaolin feed is preferably dry-milled prior to the reaction- step with the metal chloride.
• the metal chloride utilized in the invention can be one or more of the chlorides having the general formula MC1 X , where M is Si, Ti or Al; and x is 3 or 4 in accordance with M.
• the quantity of metal chloride utilized is preferably from about 20 to 35 pounds per ton of dry mixture. More generally at least 10 lbs. per ton of the metal chloride can be used, with the level selected depending upon the desired scattering improvement, except that a plateau is reached about 35' to 40 lbs/ton, above which scattering increases are very limited.
• a fine particle size kaolin preferably one in which the particle size distribution is such that from about 70 to about 100% by weight of same are of less than one micrometer E.S.D. (equiva ⁇ lent spherical diameter).
• E.S.D. equiva ⁇ lent spherical diameter
• coarser feeds can be effectively utilized, e.g., up to 70% by weight less than 2 micrometers E.S.D.
• an aggre ⁇ gation enhancing agent is selected from one or more members of the group consisting of the alkaline earth metal car- bonates or hydroxides, or lithium carbonate.
• the aggregation enhancing agent mixed with the kaolin preferably should provide from about 5 to 120 millimoles of alkaline earth metal or lithium ions per 100 parts by weight of kaolin. This equates to from about 0.5 to 12% by weight kaolin of a particulate alkaline earth metal carbonate or hydrox- ide or lithium carbonate. Where the particularly preferred cal ⁇ cium carbonate or hydroxide are used, a more preferable addition range is from about 1.5 to 4% by weight of kaolin.
• the mixture of kaolin and aggregation enhancing metal ion source subjected to the reaction with, the metal chloride should have a free moisture content of between about 0.4 and 1% by weight of the total mixture.
• ammonia is desirably added at addition levels of from about 8 to 16 pounds per ton of the feed mixture, the ammonia being added to the pre ⁇ viously combined kaolin and metal chloride. Additional improve ⁇ ments in the products are found to occur when the steps of metal chloride and ammonia addition are sequentially repeated, follow ⁇ ing the initial sequence just mentioned. However, when the pig- ment products are to be used in the coating of paper, it is pre ⁇ ferred to use the ammonia treatment only after the second, sequential addition of the metal chloride.
• the kaolin utilized as a feed for the invention can be the product of wet processing, wherein various conventional beneficiation steps known to kaolin wet processing are utilized; or in accordance with a further aspect of the invention, the kaolin can be the product of air classifying a kaolin crude, preferably to at least 88% less than two micrometers — depend- ing upon the light scattering characteristics desired in the final product; except that where the product of the invention is to be used in coating - formulations, the classification is prefer ⁇ ably -to at least 94% less than 2 micrometers.
• the aggregated products of the invention are found to have a pore volume which is higher than the feed kaolin used to form same, although lower than a calcined kaolin formed from the same feed.
• the pore void volumes of products of the present invention when prepared from fine particle size feeds are found to range from 0.4 to 0.8 cmVg-
• the products of the invention are accordingly found to have increased oil absorption in comparison to the unaggregated feed, although the oil absorption is not so high as that of a calcined kaolin prepared from the same feed.
• the increased oil absorption characteristics provides enhanced printing qualities in papers in which the product is incorporated.
• the process of the invention serves to aggregate the very fine particles (i.e. the sub 0.25 micro- meter particles) present in very fine feeds of the type hereto ⁇ fore discussed.
• These minute particles can indeed serve in the aggregates as bridges between larger (e.g. micrometer-sized) particles to which they are chemically bonded.
• one im ⁇ portant advantage to the paper manufacturer is that the other- wise large percentages of troublesome extremely fine particles have been effectively removed as separate entities, but without the need for separation steps, together with the costly equip ⁇ ment required for such operations.
• the structured kaolin pigments produced by the fore- going process have been unexpectedly found to enable preparation of surprisingly improved coated papers, and paperboard products. More specifically, coating formulations providing a bulky struc ⁇ tured coating giving improved coverage, enhanced brightness, opacity and particularly gloss at given coating weights, are achieved by use of the said pigment. With respect to the final paper product, these benefits may be taken in the form of either improved sheet properties or significantly reduced coat weights.
• the resultant coated papers are found to have enhanced properties when used in the course of offset, gravure, letterpress, and similar contact printing.
• the structured kaolin pigments of the invention comprises from about 5 to 60% and preferably from about 10 to 30% by weight of the total pigment component of the coating composition.
• the balance of the pigment can comprise any of the known coating pigments, such as coating grades of kaolins, calcium carbonate, titanium dioxide, plastic pigments, etc.
• the coating compositions, in addition to the pig ⁇ ment component, include conventional components, such as an adhesive binder, dispersants, and other known additives.
• the increase in gloss in the resultant coated papers is in part a function of the particle size characteristics of the feed kaolin used to prepare the structured kaolin pigments.
• the said feed should preferably be at least 94% less than 2 micrometers E.S.D.
• Figures 1 and 2 have reference to use of the structured kaolin pigment of the invention as a filler, and Figures 3 to 12 to its use in the coating of paper.
• FIGURE 1 is a graph, illustrating the effects upon scattering properties which result from varying the level of aggregation enhancing agent in the feed mix for the process of the invention
• FIGURE 2 is a graph, illustrating the effects upon scattering properties which result from varying the fineness of the kaolin used in the feed mix for the process of the inven ⁇ tion;
• FIGURE 3 is a graph illustrating the effect on bright ⁇ ness of a coated paper sheet by varying the percent addition to a conventional kaolin pigment, Betagloss*, of a pigment desig ⁇ nated W and prepared according to the invention, in a coating composition applied to the paper, for offset printing;
• FIGURE 4 similarly shows the effect on opacity;
• FIGURE 9 is a graph showing the effect on sheet bright ⁇ ness of varying the coat weight, in g.s.m., grams per square meter, g/m ⁇ , when using coating formulations with different ratios of the pigment of the invention to the control pigment; and FIGURE 10 similarly shows the effect on gloss;
• FIGURE 11 is a graph showing the effect on sheet brightness of varying the coat weight, in g.s.m, grams per square meter, g/m ⁇ , when using coating formulations including the pig ⁇ ment of the invention, in comparison to a control pigment, where the latter is a somewhat coarser grade of coating kaolin; and FIGURE 12 similarly shows the effect on gloss. Best Modes For Carrying Out the Invention
• the said structured pigment may be produced by chemically reacting a classified and pulverized kaolin to which from about 0.4 to about 12% by weight of calcium carbonate or hydroxide has been incorporated, as an
• I aggregation enhancer with silicon tetrachloride, the latter being intermixed with the clay at room temperature (25°C) and at the rate of approximately 20 to 35 lbs. per ton of dry feed.
• the free moisture content of the feed is preferably in the range of from about 0.4% to 1% by weight. These levels are sufficient to hydrolyze the SiCl4 to initially produce mono- silicic acid, without, however, being sufficient to precipitate free silica.
• the silicon tetrachloride may be intermixed in liquid or vaporous form.
• the intermixing is effected by any suitable mixing apparatus capable of effecting rapid and intimate contact between the reactants.
• Low shear mechanical mixers including paddle mixers and other known mixing devices, are suitable for this purpose.
• the mixture of feed and silicon tetrachloride is then exposed to ammonia, e.g., by addition of gaseous ammonia at the rate of about 8 to 16 pounds per ton of feed.
• the ammonia serves to neutralize the acidic byproducts and contributes to the bond ⁇ ing process by formation of Si n -(NH) n type polymers.
• a rapid initial reaction Occurs between the kaolin particles and the reagents.
• the subsequent process of aggregation and bond formation is a relatively slow one, which levels off in about three days. Heating to temperatures of up to about 150°C after incorporation of the reagents into the feed mixture, can help to expel volatile undesired products, but such heating is not a necessary condition for the present process, which proceeds effectively without the need for any heating.
• Additional beneficiation steps can be utilized in the process prior to the intermixing of the clay with silicon tetra- chloride. Such steps will be utilized depending upon the charac ⁇ teristics of the initial crude kaolin and upon the intended end use of the resultant product. For example, if the initial crude is already of satisfactory whiteness and brightness, and is otherwise devoid of deleterious contaminants, then minimal or no such beneficiation is necessary; i.e., in many instances mere particle size classification will suffice. Among other things, it should be appreciated that since the process of the present invention does not utilize high temperature heating as occurs during calcining, impurities which are considered highly undesir ⁇ able in processing by calcining, such as glass forming oxides, are of no major concern in the present process.
• the process of this invention can be carried out, as aforementioned, without substantially altering the feed material, i.e., as would result from heating to calcin ⁇ ing temperatures, one may utilize a wide variety of crude kaolins — or more specifically one may utilize a wide variety of feed kaolins for the present process, without enormous concern for the specific impurity levels that may be present in the kaolin, such as the aforementioned glass forming oxides, iron content or the like; i.e. the primary concern is rather one with the whiteness and brightness of the feed and the abrasion proper ⁇ ties of same.
• classification of the starting crude kaolin can be an important consideration in the present invention, since as is the case in the aforementioned
• McConnell et al U.S. Patent No. 4,381,948, the resulting aggre ⁇ gates possess light scattering qualities (and consequent opacity when utilized in papers) partially as a function of the fineness and uniformity of the particles which comprise the aggregates.
• a finely classified clay fraction one e .g . where a very high percentage of same are below 1 micrometer in equivalent spherical diameter (E.S.D.) produces an unusually excellent product in the present invention for the same reasons as are set forth in the McConnell et al patent. Classification to such a fine degree may not, however, be necessary or appropri ⁇ ate where the desired end product need not have unusually high light scattering or opacifying properties.
• a feed fraction for the present process may be provided wherein at least 88% by weight of the particles are less than 2 micro ⁇ meters ESD. (Except that as aforementioned, where the product is intended for paper coating applications, the feed fraction should preferably have at least 94% by weight of the particles, less than 2 micrometers, ESD).
• Classification can be conducted by various techniques known in the art, including air classification or by aqueous classification techniques.
• the particular kaolin crude utilized may already have sufficient uniformity of particle size, and be of sufficiently fine size to begin with, that there is no essen- tial need to effect classification; i.e. the crude ' in its "natural" condition is adequately classified to achieve the results discussed above.
• classification may not be required by virtue of the diminished need for high light scattering.
• the brightness of pigment products yielded by the invention are primarily dictated by the starting crude kaolin and by the beneficiation, if any, to which the kaolin is subjected prior to being processed in accordance with the present inven ⁇ tion.
• final GE brightness can range from 75 to over 90.
• the kaolin feed for the process produc- ing the structured pigments can ha.ve a GE brightness in the range of from about 80 to 92.
• the chemical reaction step instituted by the inter ⁇ mixing of the kaolin feed mix with silicon tetrachloride, is carried out by adding the silicon tetrachloride while the mixing operation proceeds. Once the intermixing operation is completed, the resultant product is aged, preferably for a period of at least 3 days, to enhance the scattering properties of the aggre ⁇ gated kaolin particles.
• the quality of the resultant products produced by the process of the invention depend, in part, upon the physical and chemical properties of the crude kaolin serving as the source for the feed.
• a wide range of crude kaolins can be utilized in the invention.
• the crude can be processed by conventional method- ology known in the art, including by so-called “dry” processing and/or by so-called “wet” processing. Where wet processing is utilized, it can be, in some cases, limited to aqueous classifi ⁇ cation. In other instances, depending upon the nature of the- crude, and the product desired, additional known beneficiation techniques can be used to remove undesired elements or contami ⁇ nants from the kaolin. Similarly, classification can be effected as a part of the wet processing treatment.
• the crude can be blunged and dispersed, and then subjected, e.g. by cent ifug in , to a particle size separation as an aqueous slurry or dispersion, from which is recovered a slurry of the clay, wherein a desired per ⁇ centage of the particles are beneath a specified limit.
• This slurry can then be dried to produce a clay having very low mois ⁇ ture content, normally one wherein less than 1% moisture by weight is present. Drying in this instance is preferably effected by use of spray drying.
• the calcium carbonate or hydroxide addition is preferably effected by mixing in the said material prior to the spray drying.
• silicon tetrachloride is a presently preferred reagent for use in the process of the present invention.
• metal chlorides can be effectively utilized in the invention. More specifically, metal chlorides having the general formula MC1 X , where x can be 3 or 4 in accordance with M, and M is Si, Al, and/or Ti .
• the hydrolyzed products of the indicated metal chlorides have an appropriate structure as will enable them to fit within the crystalline tetrahedra structure of kaolin.
• calcium carbonate is a preferred aggregation enhancing agent for use in the process of the invention-, other alkaline earth metal carbonates or hydroxides, or lithium carbo ⁇ nate, are utilizable in the invention.
• a preferable range of addition for the aggregation enhancing agent is from 1.5 to 4% by weight of the feed mixture.
• Coarse calcium carbonates or hydroxides are less effective in the present invention, where it is preferable rather to use the so-called paper grades of fine ground or precipitated calcium carbonate, i.e. the grades of same which are used for paper filling and paper coating.
• a suitable material for use in the process of the invention is the CARBITAL 50 or CARBITAL 90 product of Atlantic Carbonates of Baltimore, Maryland. These products have respectively particle size distribution such that 50 and 90% thereof by weight are of less than 2 microns E.S.D.
• Enhancement of the present process is effected by the addition of the enhancing agent metal ion, which is believed to result in the formation of metal silicates, which function as binding agents, yielding stronger aggregates, and which also helps to neutralize the acidic by-products.
• a kaolin crude was uti ⁇ lized as a starting material, which was derived from northeast Georgia, and which comprised a very fine particle size, material.
• the GE brightness of the said crude was thus in the range of 82 to 87 (in all instances in this specification it will be under ⁇ stood that brightness values are obtained according to the standard specification established by TAPPI procedure T-646 os-75) .
• the said crude was dried, micropulverized and then air classified into a fine and a coarse fraction.
• the fine fraction was once again micropulverized, and included approximately 97% by weight of particles having an E.S.D. (equivalent spherical diameter) of less than 1 micrometer.
• E.S.D. equivalent spherical diameter
• the said fine fraction was dried at about 150°C for a period of 15 minutes to bring the moisture to about 1% or less.
• the dried and classified feed was thereupon loaded into a Waring blender.
• Liquid silicon tetrachloride was then added at the rate of 30 pounds per ton of dry clay, corresponding to approxi ⁇ mately 1.5% by weight of the clay. This addition was carried out while the Waring blender was operating, and the silicon tetrachloride was added at the rate of about 1/2 ml in 25 to 30 seconds.
• the blender was maintained operational for an addi ⁇ tional 1 to 2 minutes.
• the clay was then dried in an oven which was open to air and ambient conditions, at about 150°C for 5 minutes. No post-milling of any type was involved in the pre ⁇ sent Example.
• the pigment product yielded by this Example was sub ⁇ jected to tests to determine the light scattering coefficient of the pigment when same was used as a filler in paper at a 10% loading factor by weight. More specifically, the pigment was tested at 10% loading in Stbrafite (trademark of Nova Scotia Forest Industries) bleached sulphite pulp beaten to a CSF (Canadian Standard Freeness) of 300-350. Deionized water was used in the sheet formation, together with 20 lbs/ton alum, and Percol 292 (trademark of Allied Colloids) as a retention aid.
• This 10% value was derived by nominally loading the material at 5, 10, and 15%, obtaining the sheet scatter for the three sets of sheets, fitting the points to a straight line by a least square analysis, and calculating the 10% level by the equa ⁇ tion generated.
• Alphatex ® product of Anglo-American Clays Corporation was used at 10% loading under otherwise identical conditions.
• the average scattering coeffi ⁇ cient determined with the use of Alphatex ® was 720 to 730 cm ⁇ /gram.
• a further control was determined by evaluating the scattering coefficient for the starting feed material, i.e. the classified clay fraction utilized in the present Example, i.e. without the chemical aggregation. When prepared under identical conditions as aforementioned, it displayed a scattering coeffi- cient of 528 cmVgram.
• Example II the same general procedure was uti ⁇ lized as in Example I.
• the starting feed material was a Georgia kaolin having a crude GE brightness of 87 to 88, which had been wet classified to 97% less than one micrometer E.S.D., and to 100% less than 2 micrometers E.S.D., and spray-dried.
• the procedure utilized in adding the metal chloride and evaluating the samples were similar to that of Example I, and two further metal chlorides were evaluated, i.e., titanium chloride and anhydrous aluminum chloride.
• the pigment products yielded in this Example were subjected to tests in accordance with the pro ⁇ cedure of Example I, and the scattering coefficients were evalu ⁇ ated at 10% filler level.
• Samples of the aforementioned Alpha ⁇ tex ® were also evaluated for comparison, and samples of the same feed were also evaluated as fillers without being subjected to the aggregation process of the invention. It was found that the untreated samples produced a scattering coefficient of 540 cm ⁇ /gram.
• the product prepared with silicon tetrachloride had a scattering coefficient of 555 cm ⁇ /gram, the product prepared with titanium chloride a scattering cross-section of 556 cmVgram; and the product prepared with aluminum chloride, a scattering cross- section of 548 cm 2 /gram.
• the Alphatex ® product had a scattering of 689 cmVgram.
• Example II The crude used in this Example was the same as that of Example I, except that the crude. as wet-classified to 96% less than 2 micrometers to provide the feed for testing.
• the said feed samples were processed with silicon tetrachloride according to the procedure of Example I, except that following the inter ⁇ mixing of the feed with silicon tetrachlo ide the mixture was exposed to a slight vacuum and was then reacted with 12 pounds of gaseous ammonia per ton of clay. The sequence of silicon tetrachloride and ammonia addition was repeated, and the result- ant product dried at 150°C.
• the Alphatex ® filled samples at 10% filler had a scattering coefficient of 700 cm ⁇ /gram, and in each series in which Alphatex® differed from 700, the scattering coefficients of the experimental sam- pies were accordingly adjusted proportionally to the adjust ⁇ ments which the Al ⁇ hatex ® -containing paper required to "bring its value to 700 cm2/gram.
• This procedure which was used in subse ⁇ quent examples, is from time to time referred to in the speci ⁇ fication as "normalizing" the scattering coefficients.
• the crude kaolin utilized in this Example was a blend of northeast Georgia Kaolins of fine particle size and G.E. brightness of about 87.
• the said crude was wet-classified to 96% less than 2 micrometers, and was then processed in a man ⁇ ner substantially identical to the samples of Example III, except that the metal chloride was titanium chloride, which was added at a dosage rate of 20 pounds per ton of feed clay. Ammonia was added as in Example III.
• the resultant products were then evaluated at 10% filler as aforementioned. It was found that the scatter levels achieved at the mentioned filler level was 544 c Vg • A control sample not subjected to the process of the invention, displayed a scatter of 522 cm 2 /g when similarly processed.
• Feed clays were prepared as described in Example II. These clays were treated with various rapidly hydrolyzing metal chlorides, at addition levels of 30 lbs/ton of clay.
• the chlo- rides used were titanium tetrachloride, anhydrous aluminum chlo ⁇ ride, and silicon tetrachloride, as described in Example III. Aggregation was found to occur with all of these metal chlorides.
• Example II The same crude kaolin as in Example I was used to pre ⁇ pare feed samples as in Example III. Moisture levels in the final feed were adjusted to be in the range of 0.05% to 3.0% by weight, and the resultant samples were evaluated as in Example I. The scattering coefficient improvements at 10% loading were evaluated, and are shown in Table II as a function of moisture levels. The .Table sets forth the increase in scattering over that yielded by an untreated sample of feed kaolin.
• the kaolin feed was a blend of two fine northeastern Georgia Kaolins.
• the feed was wet-classified to 96% less than 2 micrometers.
• the beneficiated, spray-dried and pulverized feed kaolin was mixed with 3% calcium carbonate dry weight, in slurry form.
• the calcium carbonate was a paper coating grade having a 90% less than 2 micrometers by weight P.S.D.
• the feed mixture was dried at 150°C for 5 minutes, to bring the moisture level to about 0.7%, and pulverized once more, Samples of this feed were treated with silicon tetrachloride and ammonia, and other samples with titanium chloride and ammonia according to Example IV.
• the resultant products displayed at 10% filling, light scattering of 588 and 576 cm 2 /gram, respect ⁇ ively for the silicon tetrachloride and for the titanium tetra ⁇ chloride prepared products.
• the untreated feed samples for the SiCl4 test had a scatter of 528, and for the TiCl4 had a scatter of about 522 cm 2 /g.
• Feed kaolins were prepared as in Example VII, incorpo ⁇ rating varying amounts of the aforementioned calcium carbonate in the range of from about 0 to 12% by weight of the total feed mixtu,re.
• the calcium carbonate used was in 75% solids slurry form.
• the light scatter improved with the level of calcium car ⁇ bonate addition, and is depicted in the graph of Figure 1, which shows scatter coefficient as a function of calcium carbonate addition level.
• Example VIII The procedure described in Example VIII was repeated with varying dosages of the silicon tetrachloride, ranging from 15 lbs/ton to 35 lbs/ton of feed. For a given feed clay, aggre- gation and light scatter was found to increase with the amount of silicon tetrachloride utilized.
• the feed containing 3% cal ⁇ cium carbonate had a resultant light scatter when used at 10% filler of 585 and 610 cmVgram when treated with 15 and 30 lbs/ton silicon tetrachloride, respectively. The scatter was found to be somewhat further improved by application of much higher dosage levels. Thus, at 300 lbs/ton of silicon tetrachloride, scatter at 10% filling was 630 cm 2 /gram.
• Example VII The procedure described in Example VII was repeated utilizing calcium carbonate of various fineness of particle sizes in the range of 10% less than 2 micrometers by weight to 90% less than 2 micrometers by weight. In general, it was found that in this range of calcium carbonate particle size there was little variation in achieved scatter improvement — the scattering co'efficient improvements due to the addition of the CaC03 ranged from about 35 to 55 units. For paper industry applications, it is, however, preferable to use a finer grade of calcium carbo- nate, typically 90% less than 2 micrometers, to reduce abrasion in the event any residual materials remain in the final products of the invention.
• Example VII A series of samples were prepared using starting kaolin crudes and general procedures as in Example VII, and various aggregation enhancing agents were used, including calcium hydrox ⁇ ide, barium carbonate, magnesium carbonate, and lithium carbo ⁇ nate. In each instance, the enhancing agent was added at 3% dosage level, and the test samples were processed and evaluated as in the procedures in Example VII. The resulting data, appear in Table III below.
• feed kaolins derived from the crudes used in Example IV were wet-classi ied in the range of 88% less than 2 micrometers to 100% less than 2 micrometers.
• the classified feeds were then spray-dried, blended with 3% calcium carbonate slurry, and subjected to reactants according to the procedure of Example VII.
• the uppermost curve in Figure 2 depicts the variation in scattering properties as a function of particle size. Scatter generally increased with the fineness of the feed clay. It will be noted, however, that even with a somewhat coarser feed (e.g. 88% less than 2 micrometers) good results are achieved.
• scatter coefficients for the kaolin without the added calcium carbonate, and for the feed kaolin containing the calcium carbonate are also shown.
• the process of the present invention is one which pro- vide porous structured aggregates. Aggregates thus produced by the procedures of Examples I and IV were analyzed for pore void volume by use of mercury porosimetry. The sample with higher measured porosity was deemed to have the higher intraaggregate pore void volume. Results are set forth in Table IV. The scat- ters were in the range of 585 to 630 cm 2 /g and pore void volume ranged from about 0.4 to 0.7 cm g.
• Example IV 0.635 623 2
• Example IV 0.685 630 3
• Example I 0.378 585
• Example I 0.530 608 5
• Example IV 0.660 606
• Example XIV
• Example VII The same feed as described in Example VII, was milled several times, specifically 2 to 8 times, using a micropulver- izer.
• the resultant feed samples were treated by the procedure of Example VII. It was found that increasing the number of passes through the icromill led to enhanced light scatter for the aggregated products. Specifically, utilizing 2, 4, 6 and 8 passes, provided light scatter respectively of 583, 595, 598 and 606 cmVgram.
• Example XVII illustrates the effects of aging upon the resultant products of the invention.
• struc ⁇ tured kaolin products prepared by the procedure of Example III were allowed to age for various lengths of time, after which the light scattering increases were evaluated at a 10% filler level.
• no heating or drying was utilized, but simply the aging of the intermixed metal chloride and feed.
• the light scatter was found to increase with time, and reached a plateau level after approximately three days. Specifically, scatter in a representative sample increased from 585 to 600 cmVgram, by increasing the aging period of the product from 1 day to 3 days at room temperature.
• This Example demonstrates the use of a structured kaolin pigment, prepared according to the invention, and desig- nated here as "Pigment W" to enhance the brightness, opacity, and gloss of an offset coating formulation.
• the Pigment W - was prepared according to the procedures of Example III, using a kaolin feed as in Example VII.
• the said pigment was found to possess unique properties in its ability to enhance the coverage of a paper coating.
• Beta- gloss ® a regular brightness fine #1 coating clay
• the essential ingredients of a coating formulation are a pigment and an adhesive binder, with minor amounts of other ingredients.
• the formulation used comprised:
• **coating lubricant, product of Diamond Shamrock The coating formulation was prepared by mixing the ingredients in the following order of addition. Mix coating clay in water, followed by Pigment W, and mix to 45°C. Add dispersant, (Dispex® N-40, trademark of Allied Colloids, Great Britain for sodium polyacrylate) , starch, calcium stearate, insolubilizer and latex. The amount of dispersant was controlled to give appropri ⁇ ate rheology. The solids in the coating formulation were nearly 62% by weight, as determined by moisture balance.
• the control coating formulation employed Betagloss® (BG) as the sole pigment.
• BG Betagloss®
• other coat ⁇ ings were prepared with addition of 10, 20, and 30% of pigment W to the Betagloss.
• pigment W in this Example required additional quantities of dis- persants (up to 1%), and coating formulation solids were reduced to maintain a usable rheology.
• the control coat ⁇ ing formulation had a solids content of up to 4% higher than the coating formulation with pigment W.
• Coatings were applied on a publication base stock (brightness 67, opacity 90.6, gloss 6) using a coating machine, the Helicoater, running at 1500 ft/ in for a target coat weight of 8 gsm (grams per square meter) .
• the Helicoater is a pilot blade coater, details of which are described in N.O. Clark, et al. Paper Trade Journal, September 19, 1966.
• the conditioned coated papers were calendered for 10 nips at 1500 psi and 150°F. It was found that the pigment responds to calendering very well to give good gloss properties. Also, it responded at lower pressure than usual.
• Bas is We ight - 43. 8 gsm 0.5 m/sec. printing speed Constant Mode
• K&N (a measurement of ink receptivity) shows an increase with addition of Pigment W, and further indicates the development of a more open coating structure (Figure 8) .
• Example XVI further paper coating formulations were prepared which included the same components specified in Example XVI, except that the control pigment instead of being a fine size coating kaolin such as Betagloss ® , was a coarser grade coating kaolin, comprising 50 parts of a No. 2 coating kaolin (the KCS product f Georgia Kaolin Co.) and 50 parts Of an 80% below 2 micrometers delaminated kaolin (the Alphaplate® product of Anglo-American Clays Corporation) . The control formulation was coated at 62% solids.
• the control pigment instead of being a fine size coating kaolin such as Betagloss ®
• the control formulation was coated at 62% solids.
• Example XVI 20 parts of pig ⁇ ment W, as in Example XVI, were substituted, i.e. to provide a ratio of 20 parts W to 40 parts No. 2 coating clay, and 40 parts of the Alphaplate ® .
• the second test formulation, (B) the same ratio was used, except that instead of being blended into the coating formulation as pigment powders, the pigment W was added as a 50% solids slurry, which therefore included small amounts of additional dispersants (13 lbs/ton dry clay of carboxy methyl cellulose (CMC) , 10 lbs/ton of TSPP, (tetrasodium pyro- phosphate) and 10 lbs/ton of Dispex ® N-40) .
• CMC carboxy methyl cellulose
• TSPP tetrasodium pyro- phosphate
• 10 lbs/ton of Dispex ® N-40 The test formula ⁇ tions were coated at 58% solids.
• test formulation (D) was coated at about 62% solids with 10 parts of pigment W and 45 parts of KCS and 45 parts Alphaplate ® .
• aqueous slurries In order to effectively utilize the pigments of the invention in coating applications, it is often desirable to pre- pare same in the form of aqueous slurries.
• the presence of vari ⁇ ous inorganic salts as a result of the processes of preparation of the pigments tend to produce some difficulties in making up a slurry by use of conventional dispersing agents and techniques.
• it has been found that fully satisfactory aqueous slurries can, however, be prepared by use of a combination of several dispersing agents, which have not commonly been " used in these co ' mbinations hereto- fore.

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• 1986
  • 1986-01-27 EP EP19860901194 patent/EP0230425A4/de not_active Ceased
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