HIGH PERFORMANCE PIGMENTS OF LOW OIL ABSORPTION: PREPARATION, PROPERTIES AND END-USE APPLICATIONS

Abstract: Sodium aluminosilicates (SAMS) are produced by silicate/clay reactions under hydrothermal conditions, the SAMS being characterized by low oil absorption values and high total pore volumes. The SAMS products are useful as coating pigments for paper, paper fillers and paint pigments.

Description: HIGH PERFORMANCE PIGMENTS OF LOW OIL ABSORPTION; PREPARATION, PROPERTIES AND END-USE APPLICATIONS Related and Prior Art The pigments described herein are synthetic sodium aluminosilicate compositions (SAMS) prepared from the hydrothermal reaction of select kaolin clays with sodium silicates. The products of this invention are "unique" in that they offer high performance properties despite their low oil absorption characteristics. Literature relevant to discussing these new pigment • technology is cited below: (1) S.K. Wason, U.S. Patents Nos. 4,812,299 and 4,863,796 (1989) and references cited therein. (2) S.K. Wason, J. Soc. Cosmet. Chem., 29:497-521 (Aug., 1978). (3) P. Lepoutre, N. Pauler, B. Alince and M. Rigdahl, J. Of Pulp and Paper Science: Vol. 15, No. 5, 183 (1989). (4) R. E. Hardy and G.M. Freeman: TAPPI Coating Conference Proceedings, 147-153 (May, 1989). Description of Inventive Concept; A method for preparing high performance SAMS pigments with low oil absorption properties is disclosed. These SAMS products are still produced by sodium silicate/clay reactions conducted under hydrothermal conditions as generally disclosed in U.S. Patents 4,812,299 and 4,863,796. However, they represent a significant refinement in the art and can be thought of as a more preferred embodiment of the earlier Wason patents. In particular, the SAMS earlier Wason patents. In particular, the SAMS products of this invention represent an anomaly to the prior art knowledge in that they offer superior performance properties, yet have low oil absorption values. In the prior art, SAMS performance properties were equated directly to structure as defined by a set of oil absorption criteria. In this invention, a new definition of SAMS pigment structure derived from porosimetry based principles is proposed that offers a more universal unders anding of pigment structure/property relationships. Applying these new structure principles, a select and unobvious combination of reaction parameters were identified and then utilized to yield SAMS type pigments having some unique structural properties as follows: 1. A pore structure which has very high total pore volume (exceeding 2.5 ml/gm in the most preferred embodiment of the invention). 2. A relatively narrow pore size distribution that is centered near a pore diameter of 0.3 micron (which is the optimal porosity design for efficient scattering of visible light). 3. An oil absorption value that is less than 115 gm/100 gm despite their high pore volume content (this insures improved wet-out and slurry rheology properties versus the Samtone 581 product). 4. A product particle size that falls within the range of 78-90% -2 microns (a 0.5-0.7 micron average particle diameter) as determined by x-ray sedigraph. It should be noted that many structured SAMS pigments of the prior art have pore volumes greater than 2.5 ml/gm; but clearly failed to simultaneously meet the last three criteria summarized above. To produce SAMS pigments having the unique total combination of structural properties set forth in this invention, several advancements in the hydrothermal reaction process had to be realized. In particular, the important role that reactor mixing intensity plays in determining pore structure and particle size properties had to be discovered and then utilized to help fine tune final SAMS properties. Secondly, upon scale-up to production, the steam addition rate used in bringing the reactor up to its operating temperature and pressure was found to be critical. Needed adjustments in product particle size were eventually realized by properly controlling the steam flow profile. This was accomplished by using an automated steam flow control valve system. Additionally, reactor solids have to be precisely chosen for each Base/Clay combination to yield the required pore size distribution properties. Changes in reaction solids of even 2%, very often had profound influences on pigment structure. The importance of these reaction parameters was not recognized in the prior art process. Brief Description of Drawings Reference is now made to the drawings accompanying the application wherein: Figures 1, 2, 6 and 9 are pore size distribution curves which are plots of log differential intrusion versus pore diameter; Figures 3 and 4 are curves showing the effect of clay particle size and are plots of cumulative pore volume versus pore diameter; Figures 5 and 8 are curves showing cumulative pore volume versus diameter for different reaction solids contents and a prior art comparison, respectively; Figure 7 is a plot of reactor profile comparing steam flow, reactor pressure and time; Figure 10 shows four photomicrographs of SAMS products; Figure 11 is a diffraction pattern showing a product of the invention and a prior art product; and Figure 12 is an x-ray diffraction pattern of the SAMS product of Example 5. Preferred Embodiments The present invention is further illustrated by the following examples, which should be regarded as demonstrating only some of the preferred embodiments and not limiting thereof. In the examples reference is made to the following trademarked products: (1) Hydragloss™ 90 - a fine particle size refined East Georgia clay product useful as a paper filler, the 90 indicating a GE brightness of greater than 90, available from J.M. Huber Corporation. (2) SAMTONE 581 - a paper coating available from J.M. Huber Corporation. (3) Hydragloss™ - fine particle East Georgia refined clay used as a paper filler or coating, available from J.M. Huber Corporation. (4) Hydrafine™ 90 - Delaminated clay useful as paper filler or coating, available from J.M. Huber Corporation. (5) Hydrasperse™ 90 - a fine particle refined Georgia clay paper filler or coating, available from J.M. Huber Corporation. (6) Ansilex 93 - a calcined clay paper coating, available commercially from Engelhard Corporation. The SAMS products of the present invention are characterized by the following empirical formula in 387 terms of oxide constituents: (0.01-0.5)Na 2 0 : AI2O3 : (2.01-3.0)SiO 2 : (1.0-3.0) H 2 0, by having an oil absorption capacity of less than 115 gm/100 gm while simultaneously possessing a total pore volume of at least 2.0 ml/gm, and wherein the pigment pore volume will consist entirely of pore diameter size between 0.2 and 0.7 microns, more ideally near 0.3 microns. SAMS products of this invention are produced using a carefully controlled combination of reaction conditions utilizing the following batch reaction mixture: (0.2-0.5) Na 0 : Al 2 0 : Al 2 θ3 : (2.30-2.83) Si0 2 , a ratio of sodium silicate (B) to clay (C) in the reaction mixture of 0.1:1 to 0.5:1, and a Si0 /Na 2 0 mole ratio in the batch ranging from 1.0:1 to 3.33:1, respectively. In the reaction, use of high mole ratio silicates requires a B/C molar ratio of 0.2, use of medium mole ratio silicates requires a B/C molar ratio of 0.2-0.3, and use of low mole ratio silicates requires a B/C ratio of 0.3-0.5. High mole ratio silicates are defined herein as Si0 2 /Na 2 0 ratios of 2.6-3.5, preferably 3.1-3.4. Medium mole ratio silicates are defined as having Si0 2 /Na 2 0 mole ratios ranging from 2.0-2.5. Low mole ratio silicates are defined as having Si0 2 /Na 0 mole ratios as those ranging from 1.0-1.9. The present invention also provides paper products containing the SAMS product of this invention as coating pigments and paper fillers. The coating pigments and fillers of this invention are used in accordance with procedures known to the art. The SAMS products of the invention are also useful in paints as paint pigments for both oil-based and water-based paints. The SAMS products of the invention are also useful as rubber pigments to provide reinforcement properties. The present invention also provides a method for the preparation of the novel SAMS products of the present invention which comprises reacting sodium silicate with clay under hydrothermal conditions wherein the ratio of B (sodium silicate) to C (clay) ranges from 0.1 up to 0.5 and wherein high mole ratio silicates require a B/C ratio of 0.2, medium mole ratio silicates require a B/C ratio of 0.2 to 0.3. and low mole ratio silicates require a B/C ratio of 0.3 to 0.5. and further provided that the batch composition during the reaction will be expressed by the following stoichiometric ranges: (0.2-0.5) Na 2 0 : Al 2 θ3 : (2.30-2.83) Si0 2 and recovering the product. Example 1 In this example, a systematic study of SAMS products prepared from sodium silicate/Hydragloss™ 90 reactions conducted under hydrothermal conditions was undertaken. The purpose of this study was to demonstrate the unique relationship between silicate type and Base/Clay ratio as required to yield SAMS products of this invention. The complete matrix of reactions investigated is summarized in Table 1-A. As shown there, sodium silicate reagents ranging in Si0 2 /Na 2 0 mole ratio composition from 3.33 to 1.0 were studied at various B/C molar ratios. A table detailing the composition and properties of the various sodium silicate reagents available from PQ Corporation (United States) is enclosed as Table 1-D. In all cases, the SAMS reactions of Table 1-A were conducted at 12% solids in a 2-gallon laboratory Parr Reactor using 120 psig (172°C) conditions over a one- hour cook period and a constant mixing speed of 250 rpm. The total reaction batch weight always equalled 5600 gm. On that basis, for example, the reaction of N-silicate with Hydragloss™ 90 clay at a 0.1 B/C molar ratio required the following batch recipe: Step 1 610.05 gm of active Hydragloss 90 spray- dried clay was made down in water at 50% solids using a Waring blender. Step 2A sodium silicate solution was prepared by combining 164.8 gm of N-silicate reagent (as received) and 4215.1 gm of water. Step 3 The hydragloss 90 clay slurry and sodium silicate solution were combined, mixed well and then charged to the Parr reactor for subsequent heating at 175°C. The remaining reactions outlined in Table 1-A were put together in a fully analogous fashion. Upon completing the one hour cook period at 120 psig (172°C), each product slurry was cooled to about 65°C and filtered on a Buchner funnel. The filter cake material was washed with three volumes of water and subsequently re-dispersed under low shear at approximately 20% solids for spray-drying in a Nichols Model 53 dryer. The spray-dried products were then subjected to a full battery of physical property tests, such as percent brightness, sedigraph particle size, oil absorption and pore volume analysis by mercury intrusion. The mercury porosimetry data, in particular total pore volume and pore size distribution, are important in accessing the potential optical functionality of structured SAMS pigments. In the prior art mentioned above, Wason et al, U.S. Patent No. 4,812,299 and J. Soc. fCosmet Chem. 29:497- 521 (1978), the structural characteristics of silica and silicate pigments have been loosely defined in terms of a set of oil absorption criteria. That method attempts to classify the gross structure level of a pigment on the basis of that pigment's oil absorption capacity (see Table 1-B for classifications). An inherent implication of this structure concept has been that pigments of high structure (i.e., high oil absorption) are thought to offer more performance functionality than pigments of low oil absorption (U.S. patent 4,812,299). Using that basic guideline, the SAMS reaction products representing the preferred embodiment of the prior art were engineered with respect to maximizing their oil absorption capacity. It is now apparent that SAMS pigment structure cannot be properly defined by oil absorption values. The method falsely assumes that all pigment porosity is accessible to oil penetration through capillary type action. Oil absorption measurements of pigment structure provide a relative assessment of pore volume, but wherein only certain pores of sufficient diameter to accommodate oil are actually accounted for. Data presented later in Example 5 indicate that oil absorption measurements neglect large portions of pigments porosity that are very important to light scattering efficiency. Another inherent weakness of the oil absorption methodology is that no information is obtained concerning average pore size or pore size distribution. A more universal understanding of property/structure relationships in SAMS products has been gained by collecting total pore volume and pore size distribution information by mercury intrusion and comparing structural characteristics on that basis. The gross structure level of a SAMS pigment is defined here on the basis of its total pore volume (see Table 1-B for the various structure classifications). From prior art optical considerations discussed elsewhere (Le Poutre et al) f it follows that the total pore volume and particularly the pore size distribution of a given microvoid structure should be related to overall pigment performance. Optical theory indicates that for a porous medium of 1.5 refractive index that microvoids of 0.2-0.7 micron diameter are needed for efficient scattering of visible light. Optimal scattering efficiency is provided by microvoids of uniform 0.3 micron diameter. Working under these theoretical premises, a class of unique SAMS compositions exhibiting enhanced performance properties can be engineered by the proper selection of various reaction parameters. Important SAMS reaction parameters include the following: - Hydrous clay feedstock (starting particle size) - Molar ratio composition of sodium silicate - Base/Clay molar ratio - Reaction time - Reaction temperature/pressure - Reaction solids - Reactor mixing intensity - Steam addition profile In particular, the specific influence of mixing intensity, percent reaction solids and steam addition profile on SAMS structure and particle size properties was not recognized in the prior art process. These process related points will be illustrated in more detail in later examples. In short, the present invention provides SAMS compositions and improved methods for their preparation which are unique and whose performance properties would be unexpected in view of the prior art knowledge. From the large matrix of reactions examined per Table 1-A) , those which produced SAMS products that illustrate the general embodiment of this invention are listed in Table 1-C. The respective physical properties of these products are summarized in Table 1- C as well. The physical property criteria used to describe SAMS compositions of this invention are as ollows: 1. The SAMS products will have an oil absorption capacity less than 115 gm/100 gm, while simultaneously possessing a total pore volume of at least 2.0 ml/gm. It is extremely important that the SAMS products have an oil absorption capacity less than 115 gm/100 gm for assuring acceptable wet-out and rheological behavior when producing aqueous product slurries. A main objective of this SAMS invention was to develop a functional equivalent to Samtone 581, a sodium alumino silicate paper coating, that also had the capability of being shipped to customers in bulk as a high solids • slurry. Samtone 581 cannot be slurried at 50% solids unless the functionality of the slurry product is significantly reduced by large additions of fine particle size hydrous clay which serves solely as a rheological additive (see Example 6) . The ability to produce a SAMS product slurry of at least 50% solids was of commercial importance since large volume customers (particularly paper mills) were in most cases unwilling to buy dry products in bags or sacks. Extensive labor costs arise when dry bag product must be "made down" on site at the customer's facility. It should also be noted that slurry solids of 50% or greater are needed, otherwise freight rates become cost prohibitive. Likewise, Samtone 581 (unlike calcined clay) could not be supplied to customers in bulk sparger cars because of its poor wet-out properties Therefore, it became necessary to develop a second generation low oil absorption SAMS product offering bulk slurry capabilities yet maintaining high pigment performance attributes in the end use applciations. To offer good optical performance, SAMS structured pigments must still contain a total pore volume of at least 2.0 ml/gm. The high pore volume of such products enhances the optical efficiency of various paper and costing systems by increasing the number of microvoids present to scatter visible light. It should also be noted that lowering the oil absorption properties of SAMS and thus improving its rheology has other practical ramifications. For example, better rheology enables higher SAMS pigment loadings to be used in paper coatings formulations that are to be applied to paper under high shear type conditions. 2. In a more preferred embodiment of the present invention, SAMS pigments with an oil absorption less than 115 gm/100 gm possess a total pore volume of at least 2.0 ml/gm but wherein the pigment pore volume consists entirely of pore diameters sized between 0.2- 0.7 micron or more ideally near 0.3 micron. Based on the optical considerations discussed earlier, microvoids having diameters comparable in size to the wavelength range of visible light should be the most efficient light scatterers. On this basis, the matrix of reactions suited to yielding SAMS pigments of superior optical performance is reduced considerably in scope. Several of the reaction products listed in Table 1-C do not meet the more stringent criteria of the preferred embodiment (see footnote section of Table 1-C). Nonetheless, reaction products satisfying the preferred embodiment criteria can still be produced from sodium silicate reagents ranging in Si0 /Na 0 mole ratio composition from 1.0 to 3.33. However, the exact Base/Clay reaction ratio requirements vary substantially from one silicate type to another. The silicate plus Base/Clay ratio combinations producing preferred SAMS product compositions can be generally summarized as follows: REQUIRED B/C SODIUM SILICATE TYPE MOLAR RATIO For high mole ratio silicates 0.2 (N @ 3.33 Si0 2 /Na 2 0) For medium mole ratio silicates 0.2 - 0.3 (D & RU, from 2.0-2.5 Si0 2 /Na 2 0) For low mole ratio silicates 0.3 - 0.5 (meta & BW, from 1.0-1.7 Si0 /Na 2 0) For the above SAMS reactions, the associated batch compositions can be generically expressed by the following stoichiometric ranges: (0.2-0.5) Na 0 : AI2O3 : (2.30-2.83) Si0 2 This scheme is intended to be a general guideline on preferred silicate plus B/C ratio combinations rather than an absolute one, since other reaction parameters do have some influence on resulting pore structure properties as well. To better understand the inter- dependent relationship between silicate mole ratio composition and B/C reaction ratio as pertaining to SAMS pore structure, one has to only examine the pore size distribution curves of Figures 1 and 2 respectively. In these figures, the plots of log differential intrusion versus pore diameter are used to illustrate changes in relative pore size distribution. In Figure 1, the pore size distributions for several SAMS products of 0.3 B/C ratio are compared that were produced from different sodium silicate reagents. These curves show that the pore size distribution broadens significantly towards larger pore diameters as the sodium silicate mole ratio composition increased from 1.0 to 3.33. A similar systematic broadening of pore size distribution towards larger pore diameters can also be observed in Figure 2 as higher B/C reaction ratios are employed. In Figure 2, SAMS products consisting of BW-50 silicate and Hydragloss 90 clay at B/C molar ratios of .3, .4 and .6 are compared. In both test scenarios, the reaction solids were maintained at 12%. The pore distribution curves of Figures 1 and 2 show why lower B/C reaction ratios are needed when sodium silicate reagents of higher mole ratio composition are selected for use. 3. In the most preferred embodiment of the present invention, SAMS pigments having an oil absorption less than 115 gm/100 gm would possess a total pore volume exceeding 2.5 ml/gm wherein the pores would have nearly uniform pore size diameter of 0.3 micron for providing optimal light scattering properties. None of the SAMS products listed in Table 1-C meet these new criteria; however, such products can be produced once other reaction parameters beyond silicate type and B/C ratio are taken into consideration and fully optimized. The SAMS pigment that will be presented in Example 5 fulfills the above criteria and represents the most "state of the art" product. Once the influence from other reaction parameters is fully taken into account, then some distinct preferences arise among the available silicate reagents used in producing SAMS products. Sodium silicates having a Si0 2 /Na 0 mole ratio composition of about 2.06 are most highly preferred for the following reasons: a. Sodium silicates of higher mole ratio composition (particularly N at 3.33 M.R. ) have a greater propensity to yield SAMS products of coarser particle size and also higher oil absorption. These properties result from the higher silica contents provided by such sodium silicate reagents. Both of these trends are in opposition to the desired SAMS pigment properties. b. Sodium silicates of very low mole ratio composition (like meta at 1.0 M.R.) require somewhat higher Base/Clay reaction ratios to yield a functionally equivalent SAMS product. U sing greater amounts of silicate reagent is undesirable from the standpoint of increasing the manufacturing costs. 87 TABLE I -A A Study of Sodium Silicate/Hydragloss 90 Clay Reactions Conducted Under Hydrothermal Conditions Sodium Silicate Reagent* Base/Clay Molar Reaction Reacted with HG-90 Clav Ratios Examined Solids,**% N (3.33 Si0 /Na 2 0 M.R.) RU (2.47 Si0 2 /Na 2 0 M.R.) D (2.06 Si0 2 /Na 2 0 M.R.) BW-50 (2.06 Si 2 0/Na 2 0 M.R.) Meta (1.0 Si0 /Na 2 0 M.R.) Note: *A11 sodium silicates shown here are commercially available from PQ Corporation. The SiO /Na 2 0 mole ratio composition of each silicate is shown in parenthesis. **The hydrothermal conditions utilized in these reactions were as follows: - 120 psig (172° c ), - 1 hour cook time, - 250 rpm mix speed in a 2- gallon laboratory Parr reactor TABLE 1-B Comparison of Pigment Structure Definitions : Oil Absorption versus Pore Volume VHS (Very High Structure) Above 200 Above 3.3 HS (High Structure) 175-200 2.5-3.3 MS (Medium Structure) 125-175 1.6-2.5 LS (Low Structure) 75-125 0.8-1.6 VLS (Very Low Structure) Less Than 75 Less than 0.8 Note; *Oil Absorption values determined fcy rub-out method of ASQΪ-D.281. Structure definition taken from Reference 1 and 2. **Values determined fcy Mercury Intrusion Pαrosimetry using a micrαmeritics AutoPore-II 9220 unit. Pore volumes were determined over an intrusion pressure range of 10.0 - 6,029 psia. Data were collected using an advancing contact angle of 130 degrees and a pressure equilibration time of 10 seconds per intrusion measurement point. TABLE 1-C SAMS Products Illustrative of the Invention Basic Physical Property CriLe iu: i) SAMS having an oil absorption value less than lib g/lOOg; but also having a total ι pore volume of at least 2.0 ml/g. ii) A more preferred embo iment requires that the pigment pore volume consists only 7 of pore diameters sized from 0.2 to 0.7 micron. Note: lydrot ermal reactions I o the study described in Table 1 -A. **Values determined by Mercury intrusion porosimetry. The designations sh and br denote "shoulder" and "broad distribution" respect,ively. Also, see Figures 1 and 2 for select pore sikie distribution curves. ***SΛMS products nol consistent with the more preferred embodiment of this invention ■ TABLE 1-D Example 2 This experiment illustrates the significant influence that clay feedstock particle size has on resulting SAMS product properties. In particular, the influence on SAMS pore structure and on SAMS product particle size are addressed here. In this study, low oil absorption SAMS products meeting the physical criteria of this invention were prepared from four different hydrous clay feedstocks respectively. The clay feedstocks varied in average Stokes equivalent particle diameter between 0.2 and 0.7 micron. In summation, the clay feedstocks examined represent an assortment of Number 1 and Number 2 type hydrous clay products currently marketed by J. M. Huber under the trade names Hydragloss 90, Hydragloss, Hydrafine™ 90 and Hydrasperse ,B, .90. For each clay feedstock, an analogous SAMS product was produced using a 2-gallon laboratory Parr reactor. The reactions utilized D-silicate (2.06 mole ratio composition) with the appropriate hydrous clay at a B/C molar ratio of 0.2 and 14% reactor solids. The reactions were subjected to a 120 psig (172°C) cook over one hour using a Parr mixing speed of 150 rpm. For a total batch weight of 5600 gm, this required 685.2 gm of active spray-dried clay (subsequently made down to 50% solids) to be combined with 224.0 gr of D- silicate reagent (as received) and 4,005.6 gm of dilution water to yield the desired reaction stoichiometry. The reaction products were filtered, washed and spray dried as described previously in Example 1. In accordance with Table 2, the physical properties of the various SAMS pigments indicate substantial changes in pore structure and final particle size as a function of the initial clay feedstock particle size. As the average particle size of the clay feedstock increased, there was a corresponding increase in the SAMS product particle size. At the same time, the pigment pore volume was observed to decrease and the pore size distribution shifted towards larger pore diameters. These pore structure trends are shown graphically in Figures 3 and 4 respectively. It is very interesting to note that the maxima associated with the pore size distribution curves occur at diameter sizes that closely match the average Stokes equivalent particle diameter values determined for the initial clay feedstocks. Based on the optical/light scattering concepts presented in Example 1, it is apparent that clay feedstocks of 0.2- 0.6 micron average particle diameter must be utilized to produce SAMS products with preferred properties. However, those feedstocks of 0.2-0.3 micron average 7 particle diameter are most highly preferred to use since SAMS pore diameters of similar dimension are produced. SAMS pigments offering microvoids of uniform 0.3 micron diameter are expected to be the most optically efficient. It should also be noted that the oil absorption values reported in Table 2 show very little variation; hence, defining SAMS pigment structure on the basis of oil absorption appears to hold little predictive value. TABLE 2 Low Oil Absorption SAMS* Produced from Various Clay Feedstocks Starting SAMS Clay Feedstock** Physical Property Brightness, % Specific Gravity Sedigraph Particle Size: % - 2 microns % - 1 micron % - 0.5 micron Oil Absorption, g/lOOg BET Surface Area, m 2 /g Pore Volume, ml/g (Mercury Intrusion) 2.33 2.26 2.14 2.0 Pore Size Distribution (Population Maxima) , diameter in micron 0.30 0.30 0.60 0.79 Note; * These products were produced from clay + D-Silicate reactions all conducted at a 0.2 base/clay molar ratio, 14% reaction solids, 120 psig (172°C) cook ov 1 hour and a 150 rpm Parr mix speed. ** The particle-size and brightness of the starting cla feedstocks were as follows: Brightness Hydragloss 90 Hydragloss Hydrafine 90 Hydrasperse 90 Example 3 In this example, the influence of reaction solids and of reactor mixing intensity on SAMS structure properties are examined respectively. Using the selection guidelines set forth in Example 1, D-silicate (2.06 mole ratio) was utilized in our reactions at a Base/Clay molar ratio of 0.3. In all cases, the D- silicate/clay reactions were conducted in a 2-gallon laboratory Parr reactor using a 120 psig (172°C) cook over 1 hour. Specific details concerning the other reaction parameters (such as percent reaction solids, hydrous clay feedstock, and/or Parr mixing intensity) are summarized accordingly in Table 3. All reaction batches were based on a total reactor charge of 5600 gm in analogy with Examples 1 and 2. The reaction products were also filtered, washed and spray-dried as previously described. In Part One of this study, Omnifil based SAMS products were produced at different reaction solids ranging from 10-16%. The physical properties of these reaction products indicate substantial changes in pore structure as well as final particle size as the reaction solids were changed (see Table 3) . As the reaction solids were systematically increased from 10 to finally 16% solids, there was a corresponding increase in the SAMS product particle size. At the same time, the pore size distribution was observed to broaden somewhat towards pore sizes of greater diameter. Changes in total pore volume with increasing reaction solids were also noted; however, the observed variations did not appear to assume any parallel or regular trend. The pore structure variations resulting from reactor solids changes is shown graphically in Figures 5 and 6. As seen in Figure 6, broadening of the pore size distribution was actually the result of bimodal pore character being formed as higher reaction solids were used. In designing reaction batches to produce SAMS pigments with preferred properties in accordance with this invention, care must obviously be taken in choosing the proper reaction solids. A reactor solids level that maximizes product pore volume is preferred; however, this factor must be weighed against particle size and pore size distribution considerations arising from the reaction conditions. For this reason, reactions of this invention are generally best conducted within the 10-14% solids range since product particle size is generally finer and the pore size distribution remains centered closer to a diameter size of 0.3 micron. The importance of product particle size on functional performance will be addressed in Example 4. It should again be pointed out that oil absorption methods failed to distinguish any structural differences in these SAMS products. In Part Two of this study, Hydragloss 90 based SAMS products were produced at 14% reaction solids but wherein mixing intensities ranging from 150 to 350 rpm were examined. The physical properties of these SAMS products indicate that structural changes do occur as the mixing intensity was varied. As the Parr mixing speed was increased from 150 to 250, and then finally to 350, rpm, there was a corresponding increase in the SAMS product particle size (see Table 3) . At the same time, the pigment pore volume was being substantially decreased while oil absorption capacity was actually increased. Using minimal mixing speeds to increase pigment pore volume and to lower oil absorption capacity, is an important aspect of our SAMS reaction process. Slower mixing speeds were also preferred from the standpoint of yielding SAMS products of finer particle size (around 85% -2 microns is preferred, see Example 4) . TABLE 3 I. Influence of Reaction Solids Reaction; Qtπnifil clay + D-Silicate reactions at 0.3 Base/Clay molar ratio, 120 psig (172°C) cook over 1 hour with Parr mix speed of 150 rpm and the reactor solids ranging frcm 10-16% has a 2.06 Siθ2/ a20 mole r SAMS Physical Property Brightness, % Specific Gravity Sedigraph Particle Size, % —2 microns % -1 micron % -0.5 micron Oil Absorption, G/lOOg BET Surface Area, m^/g Pore Volume, ml/g (Mercury Instruction) 2.65 2.57 2.57 2.53 Pore Size Distribution (Maxim), diameter in micron 0.37 0.39, 0.44, 0.55, 0.33 0.36 0.33 H. TnflnRnπR of Reactor Mixing Speed Reaction; Hydragloss™ 90 clay + D-Silicate reactions at 0.3 Base/Clay molar ratio, 120 psig (172°C) cook over 1 hour, 14% solids, but with the Parr mixing speed varied frαn 150, to 250 and then finally 350 rpm, respectively. D-Silicate (PQ Corp.) has a 2.06 Siθ2/Na2θ mole ratio Example 4 Using the reaction parameter concepts discussed in Examples 1-3 (concerning silicate type and B/C ratio selection, as well as percent solids, mixing intensity and clay feedstock requirements) preferred products of this invention were produced using a 250-gallon Pilot scale reactor. This high pressure reactor was equipped with a 17-inch diameter marine style impeller having variable speed capability and, in contrast to the laboratory Parr reactor, was heated entirely by internal steam sparging rather than by an external heat source. Hydrothermal reactions of Hydragloss 90 clay with D-silicate and with Meta-silicate were conducted, respectively, in accordance with the conditions outlined in Table 4-A. Reactions #1 and #2 with D- silicate were identical except for a change in reactor mixing intensity. Reactions with Meta-silicate at low and high speeds were also conducted; however, the extremely poor filtration characteristics of the resulting low speed material prevented further processing of it to a finished spray-dried product. As shown in the materials section of Table 4-A, initial batch solids in the pilot reactions had to be adjusted up to allow for some solids dilution resulting form steam condensation. Final reaction solids at operating temperature and pressure were approximately 10%. After completing the cook period, the product slurry was discharged to a drop tank and subsequently diluted with 190 gallons of fresh water. The hot slurry (65°C) was then filtered using a rotary vacuum string discharge type filter equipped with an accessory wash blanket so as to wash the filter cake material to a conductivity value of 400 mohs or less. The wash blanket was required to lower product conductivity (by removing soluble alkali) and to obtain the maximum product brightness. The SAMS filter cakes were re- dispersed at approximately 22% solids using low shear mixing and subsequently spray-dried for testing work. They physical properties of each product are also summarized in Table 4-A. The very high pore volume (greater than 2.5 ml/gm) of each product should be noted. In comparison, Samtone 581 (of the prior art) has an oil absorption value of about 150 gm/100 gm. As previously observed, a higher mixing intensity produced a SAMS product of coarser particle size (compare products #1 and 2). In Part Two of this study, the products of Table 4-A were evaluated as fillers in a wet-end paper application and as coating pigments in a L C/rotogravure type coating application. In the paper filler study, the three SAMS products were evaluated relative to a premium calcined clay control (Ansilex 93). Handsheets were prepared containing 4, 8 and 12 parts of filler respectively. Details concerning the furnish as well as the other test parameters are summarized in Table 4-B. Optical properties including corrected opacity, brightness and whiteness were determined on five handsheets formed for each test. the averaged results are also reported in Table 4-B. In terms of sheet opacity, the filler data of Table 4-B indicate that the two SAMS products of finer particle size (i.e., A and C) offer equivalent, if not generally superior, performance to calcined clay (particularly at the 12% filler level). SAMS pigment A also provided comparable brightness and whiteness values versus the calcined clay. Despite their similarities in pore structure, pigment B provided reduced opacifying properties across the board versus SAMS pigments A or C. This performance drop can be attributed to the much coarser particle size of pigment B. On this basis, the preferred average particle diameter size range for SAMS products of the present invention is 0.5-0.7 micron (by Stokes Law) or approximately 8% -2 microns. In a coating study, SAMS of reaction #3 (per Table 4-A) was compared to Samtone 581 in a LWC/roto type formulation wherein five parts of structured pigment was used in combination with 95 parts of delaminated clay. A 60/40 delaminated/#2 clay pigment combination served as a typical control formulation. Other details concerning the coating formulations or the "CLC" coating parameters are summarized in Table 4-C. The coating properties of each system are also reported there. Both SAMS containing formulations (F and G) provided superior opacity and brightness versus the control (E). In terms of opacity, sheet gloss and printed gloss properties, the SAMS of the present invention clearly out-performed Samtone 581. In particular, the improvement in opacity over Samtone 581 can be explained on the basis of superior pigment pore structure design that provides more effective scattering of visible light. The formulation containing the new SAMS also showed notable advantages versus the Samtone 581 formulation in both high shear and low shear coating viscosities, which is a direct consequence of its lower oil absorption properties. Lower coating viscosities for the new SAMS formulation (G) translated to improved runability on the "CLC" pilot coater. TABLE -A Pilot Plant Scale-Up of New Low Oil Absorption SAMS Products SAMS Reaction Products Reaction Parameters #1 #2 #3 Clay Feedstock HG-90 HG-90 HG-90 Sodium Silicate* D D Meta Base/Clay Molar Ratio 0.3 0.3 0.5 Reaction Solids, % 10 10 10 Reaction Pressure, psig 120 (172°C) 120 (172°C) 120 (172°C) Cook Time, Hrs. 1.0 1.0 1.0 Mixing Speed, rpm 41 54 54 (fpm tip speed) (182 fp ) (240 fp ) (240 fpm) Material Batch Sheet #1 #2 #3 Batch Water, lbs. 986.0 986.0 933.4 Silicate, lbs. 71.6 71.6 31.8 HG-90 Slurry (67% solids,) lbs. 217.9 217.9 200.6 Initial Solids, % 13.9 13.9 14.3 Steam Condensate, lbs. 500.2 500.2 500.2 Batch Total, lbs. 1,775.7 1,775.7 1,666.0 Note: *D-Silicate (PQ Corp.) has a 2.06 Siθ2 Na2θ mole ratio composition; meta (Metso 2048) has a 1.0 mole ratio. Product Physical Properties #1 #2 #3 Brightness, % Specific Gravity Sedigraph Particle Size, % - 2 microns % - 1 micron % - 0.5 micron Average Stokes Equivalent Particle Diameter, micron Oil Absorption, g/lOOg pigment Pore Volume, ml/g (Mercury Intrusion) 2.66 2.62 2.70 TABLE 4-B Comparative Performance of Several Low Oil Absorption SMAS Pigments in a Paper Filler Application Handsheet Parameters* Pigments: A SAMS (Rxn #1 of Table 4-A) B SAMS (Rxn #2 of Table 4-A) C SAMS (Rxn #3 of Table 4-A) D Calcined Clay (Ansilex 93) Filler Levels: 4%, 8% and 12%, respectively Furnish: 60% AO-2 (hardwood) and 40% International Pine (softwood) Freeness: 336 csf Basis Weight: 40#/ream pH: To 4.5 with Alum Retention Aid: 0.025% Betz 1260 Machine Calender: 2 Nips (weight of steel roll only) Note ♦ Handsheets were formed using Tappi Msthod T205 αn-88, rev. 1988, titled "Forming Handsheets for Physical Testing of Pulp". Results Performance of SAMS Pigments In a LWC/Rotogravure Coating Application Paper Coating Formulation (in parts E F G Delaminated Clay (Hydraprint) 60 95 95 No. 2 Kaolin Clay (Hydrasperse) 40 — — SAMTONE 581 (Medium Oil Abs. SMS Pigment)* — 5 — SAMS (from Table 4-A, Rxn Product #3, Low Oil Abs. ) Polyacrylate Dispersant SBR Latex (Dow 620) Starch (Penford Gum 295) Calcium Stearate Note: *Pigment previously described in (U.S. Patent No. 4,863,796; Exaπple TVo). Coating Conditions: Coating Solids = 60.0% Coat Weight = 6.Of/ream Basestock = 32#/ream woodfree paper Coating Ifethod = "CLC" pilot coater operating at 2500 fpm. Super Calendered - 2 nips @ 800 pli, 150°F heat. Coating Properties: Coated Sheets Property Brightness, % Gloss, % Opacity, % ICT, No. 3 ink (cm/sec) Printed Gloss, % Coating Viscosity: Brodkfield (20 rpm, No. 4 spindle), cps Hercules (4400 rpm, E-bαb), cps Example 5 In this study, the #1 reaction product of Example 4 was appropriately scaled up to a 7200-gallon high pressure reactor. A full scale production run was commences wherein water, 31,934 lbs., and D-sodium silicate, 2,040 lbs. (as received), were added to the reactor. The D-silicate reagent has a Siθ2nNa2θ mole ratio composition of 2.06 and is 44.1% active. Next, 8,015 pounds of Hydragloss 90 dispersed filter cake slurry at 51.9% solids was added. The reactor contents were continuously mixed by a mechanical agitator turning at 8 rpm (180.1 fpm tip speed) and heated to a final temperature of 175°C (130 psig) using live steam. The steam addition was accomplished by employing an internal steam sparger system. Upon reaching our operating temperature and pressure, the reaction solids had reached 10%. After heating the reaction batch at 130 psig for a total of 65 minutes, the resulting product slurry was vented into a drop tank and subsequently filtered, washed with water, redispersed and then spray-dried to a moisture content of approximately 3%. In analogy with the pilot scale work, a string discharge rotary vacuum filter equipped with an accessory was blanket was used to yield wet filter cake material having a conductivity value of 400 mohs or less. From experience we have determined that a conductivity value of 400 mohs insures that sufficient product washing has occurred to achieve the maximum possible product brightness. Given the amounts of D-silicate, Hydragloss 90 clay and water employed in this hydrothermal process, the reaction batch composition can be described as having a Base/Clay molar ratio of 0.3 at 10% solids or alternatively, in terms of the oxide constituents, as 0.30 Na 2 0 : 1 2 0 3 : 2.62 Si0 2 : 159 H 2 0 when normalized with respect to the I2O3 molar content. Our reaction product was evaluated and characterized by various test methods. The chemical and physical properties of this SAMS product are summarized in Table 5-A. Generically, the product can be described as a sodium aluminosilicate composition. The properties of the Hydragloss 90 clay feedstock as well as those of Samtone 581, per the prior SAMS art, are also listed in Table 5-A for comparative purposes. Based on the elemental analysiεt's data, the specific composition for the preferred SAMS product of this invention can be expressed in terms of its oxide constituents as 0.15 a2θ : AI2O3 : 2.34 Siθ2 2.0 H2O. In more general terms, the range of SAMS compositions within the scope of this invention is (0.01-05) Na2θ : I2O3 : (2.01-3.0) Siθ2 : (1.0- 3.0)H2θ. A Siθ2 AI2O3 mole ratio range of 2.01-3.0 is clearly unique compositionally versus the Samtone 581 product of the prior art. Samtone 581 had an oxide composition of 2.0 a2 2 0 3 3.3 SiO. 2.2 H 2 0. A critical feature of the reaction process to produce the SAMS in this example involves the careful regulation of steam flow used in bringing the reactor contents up to 130 psig (175°C). Table 5-B summarizes the hydrothermal conditions needed to produce the desired SAMS product (target particle size equals 85%- 2 microns). In an earlier production run, a coarse particle size SAMS product (70% -2 microns) was produced when a linear pressure-up profile covering 27 minutes was employed. This particle size problem remained despite further adjustments in the reactor's mechanical mixing intensity. In this reaction, downward adjustments in mixing speed below 8 rpm did not provide further decreases in SAMS product particle size. Consequently, a new pressure-up profile of reduced slope was established that extended the reactor's ramp-up time out to 35 minutes (see Figure 7) . This strategy was accomplished by setting a 55 psi intermediate pressure point whereat the steam flow was rapidly reduced by approximately 50% using an automated steam flow control valve system. These changes acted to slow down the reaction associated with aggregate formation and thereby yielded a SAMS product of finer particle size. Laboratory studies have shown that the particle size of SAMS products are largely established during the pressure-up phase and little if any changes offer after approximately 15 minutes into the cook period. It is therefore not surprising that changes in steam flow influence particle size formation. The importance of steam addition rate in controlling particle size was not recognized in the prior art production process. As can be seen in Table 5-A, the preferred SAMS product of this invention exhibits a novel combination of properties relative to the starting Hydragloss 90 clay and to the Samtone 581 product. Of particular significance is the large difference in oil absorption capacity between the new SAMS product and Samtone 581; yet, the total pore volumes of these two products as determined by mercury intrusion are virtually identical (both equalling 2.85 ml/gm). The cumulative pore volume curves for SAMS Example 5 and Samtone 581 are presented in Figure 8 for comparative purposes. Substantial differences in their intrusion profiles are evident. The differences in pore size distribution can be seen in Figure 9, which is a derivative type plot of log differential intrusion versus pore diameter (where log differential intrusion equals dV/dlogD) . From Figure 9, it is easy to explain the lower oil absorption capacity of SAMS Example 5 on the basis of its finer pore size distribution versus Samtone 581. Apparently, SAMS Example 5 has many pores that are too small to participate in oil absorption via normal capillary type action. If characterized on the basis of established oil absorption criteria (References 1- 3), SAMS Example 5 would have been classified as "low structure" when in fact it actually has a high pore volume content. Structure/oil absorption criteria would have thus incorrectly suggested that SAMS Example 5 would provide lower optical and functional properties than Samtone 581 in various end-use applciations. Applciations data are presented in the following Examples which clearly demonstrate the superior functional performance of the new SAMS products. As discussed in Example 1, a medium of 1.5 refractive index containing microvoids of uniform 0.3 micron diameter should provide optimum light scattering efficiency for visible light. It is also expected that uniform 0.3 microvoids would be more efficient than a broad type pore distribution of equivalent average size. As can be seen in Figure 9, Samtone 581 has a rather broad bimodal type pore size distribution with maxima occurring at pore diameters of 0.95 and 0.38 micron respectively. In contrast, SAMS Example 5 was engineered by synthetic means to contain a high pore volume structure having a relatively narrow pore size distribution centered very close to 0.3 micron. It is then not surprising that SAMS Example 5 should exhibit superior optical performance properties to those of the prior art. Total pore volume and pore size distribution, as determined by mercury intrusion, provide a basis for a more universal explanation of SAMS structured pigment performance than oil absorption measurements. Like Samtone 581, SAMS Example 5 appears in SEM photographs to be structured agglomerants composed of small flat platelets (see Figure 10). Likewise, the present SAMS contain remnants of altered clay platelets having an integrated rimmed area of amorphous non- diffracting alkali metal silicate-kaolin reaction product. By the term "rimmed", it is meant that the altered primary particles are comprised of a core material having an integral border or outer edge material of different constitution from the core. The primary particles are generally in the form of lamella (irregular to pseudo-hexagonal shaped plates). The rim is an outer edge or border which usually substantially encompasses the plate perimeter. By the term "amorphous" it is meant that the material does not have a characteristic x-ray diffraction pattern. When comparing the x-ray diffraction patterns of SAMS Example 5 and Samtone 581 to that of the starting Hydragloss 90 clay, attenuated kaolinite peaks arising from the kaolin clay remnants are similarly observed. However, it was quite interesting to note that SAMS of the present invention typically show lower degrees of clay platelet alteration than Samtone 581 (see Figure 11). In Figure 11, the 0,0,1 diffraction peaks of kaolinite, SAMS Example 5, and Samtone 581 (from top to bottom respectively) are compared and the relative peak heights indicate a greater percentage of kaolinite content left in- the SAMS products of Example 5. In Figure 12, a typical XRD scan of SAMS Example 5 over the two theta region from 10-40 degrees is presented showing the attentuated kaolinite pattern. The same conclusions regarding the extent of clay alteration can also be drawn by comparing the percent loss on ignition values for the two SAMS products (LOI values decrease with increasing extent of clay alteration). TABLE 5 -A Comparison of Typical Properties : Ccmmercial-Scale SAMS Products vs. Hydragloss 90 Feedstock **Tαtal pore volumes were determined over an intrusion pressure range of 10.0-6029 psia. Data were collected using an advancing contact angle of 130 deg. and a pressure equilibration time of 10 sec. per intrusion measurement point. A Micr neritics AutoPore-II 9220 pαrosimeter was used for all measurements. ★★★ Pigment of Exaπple Otøo per U.S. Patent #4,863,796. ϋhe EITe L of Reactor Steam Flow en SME Product Eαππaticn Cαimercial Scale Production of Low Oil Absorption SAMS Reaction Targeted Product SδMS w/ 70% Parameters (84% - 2m particle size^ - 2m particle size Initial Steam Flow (into reactor), lbs./hr. 30,500 30,500 Intermediate Pressure Point*, Steam Reduction 50% None (linear @ psi @ 55 psi** Pressure - up profile) Ramp-Up Time, min. 35 27 Final Cook Pressure, psig 130 130 Cook Time, min. 65 65 Reactor Mix Speed, rpm 8 8 (fpm tip speed) (100.5) (100.5) Note; *Point during the ramp up phase vfaere the steam flow is quickly reduced a set percentage fcy means of an autαiated steam control valve. **See Figure 3 for the resulting steam flow and reactor pressure profiles. Example 6 In this experiment, the superior slurry makedown and rheological properties of SAMS Example 5 versus Samtone 581 are demonstrated. Also a process is disclosed for preparing a SAMS structured pigment slurry offering high performance properties and having a 50% minimum solids. In a production scale trial, a structured pigment slurry derived from the SAMS of Example 5 was produced using a high shear Cowles, continuous makedown type process. In the makedown, a spray-dried 95/5 composite blend of SAMS/Hydragloss 90 was used for building slurry solids directly in a continuous fashion. The makedown system consisted of a 700-gallon Cowles wet-out tank used in sequence with a second Cowles mix tank of 3,000-gallon capacity. The composite slurry leaving the Cowles tank was then pumped by means of an air diaphragm pump to a large, agitated storage tank capable of holding several tank cars of product. The wet-out tank is our process was equipped with a 200 horsepower Cowles that was operated at a tip speed of 4300 fpm (3:1 tank to blade diameter ratio and no baffles). The larger mix tank was equipped with a 350 horsepower Cowles that was operated at a tip speed of 5000 fpm (4:1 tank to blade diameter ratio plus baffles) . The additional high shear mixing received in this second Cowles tank was very important as it improves product dispersion and lowers Hercules viscosity. Typically, the product throughout rate averaged 4.0 dry tons/hour. The slurry and spray-dried feedstocks utilized in this makedown process were prepared as follows. In a 150,000-gallon storage tank, 146,900 gallons of SAMS Example 5 (as dispersed filter cake slurry of 22.0% solids) was blended with 2550 gallons of 52.2% solids Hydragloss 90 dispersed filter cake slurry to yield a 95/5 dry weight ratio composite pigment slurry. This filter cake slurry blend represented 163.6 dry tons of composite pigment at 22.6% total solids. The amount of Daxad 30 organic dispersant totaled 0.03% (on active polymer basis). Approximately 75k% of our filter cake slurry blend was stray-dried using typical commercial drying conditions. The dry composite pigment was then used in combination with the remaining filter cake slurry blend to yield a final slurry product of 50% solids. Combining the dry and slurry feedstocks was accomplished by simultaneously feeding them into the Cowles wet-out tank at rates of 98 lb/min. and 16.5 gal/min. , respectively, k The dry composite pigment was metered in by means of automated dry bin/feeder system. They above feed rates translate to the formation of a 95/5 composite slurry having about 52% solids at a continuous through-put of 4.0 dry tons/hour. The makedown process was continued until 150 dry tons of slurry product had been produced (solids were verified by a specific gravity check to be 52.0%). With all the slurry product now in the large storage tank, solids were reduced to 50.0% with water and the viscosity values determined. At this juncture, the Brookfield (20 rpm) and Hercules (A-Bob) viscosities were 180 centipoise and 18+/655 rpm respectively (see Table 6- A) . The viscosity values for a Samtone 581/Hydragloss 90 clay composite slurry of 50% solids produced under similar high shear Cowles makedown conditions are presented in the table as well for comparative purposes. To achieve comparable slurry makedown and rheological properties, 20 parts of Hydragloss' 90 clay (rather than just 5) has to be used with the Samtone 581 as a rheological additive. Adding such a high percentage of Hydragloss 90 is not practical as it seriously compromises opacifying properties in many paper related applications for SAMS. The paper coating performance of our structured pigment slurry prepared from SAMS Example 5 will be addressed later in Table 6- C. Given the relatively low Brookfield viscosity of our 95/5 structured pigment slurry (180 centipoise at 20 rpm), poor slurry stability was inevitable. A stability study indicated the presence of hard sediment after only three days. Therefore, a polymeric thickening agent, preferably an alkali soluble acrylic polymer emulsion like Acrysol TT-615, was employed to improve pigment suspension properties (see Reference 7) . Good pigment suspension properties are needed when slurries are to be shipped long distances in bulk by a tank car. To the 150 dry tons of slurry produced form the original makedown process, Acrysol TT-615 polymer was subsequently added. The polymer was incorporated by means of a tank recirculation line equipped with an injection port/in-line mixer combination. In total, 180.0 active pounds of Acrysol TT-615 was added (0.06% by weight) to yield a final slurry product having a Brookfield (20 rpm) viscosity of 660 centipoise and a Hercules viscosity (in dynes) of 18+/640 rpm using the A-Bob. The slurry product thereby exhibited good stability properties over a 4-week time period and can be pumped by customers using ordinary centrifugal type pumps. Achieving a 50% solids structured pigment slurry having good stability and pumpability properties was an importance objective of this work. Based on manufacturing experience grained from additional trial runs, the typical range of properties found for the 95/5 structured pigment slurry of this invention are summarized in Table 6i-B. Finally, it should also be noted that a critical feature of the slurry process involves initial makedown to 52% solids and then diluting back to 50%; otherwise, Hercules viscosities suitable for centrifugal pumping are generally not achieved. Another important objective of this work was to produce a SAMS structured pigment slurry (as per above) offering uncompromised performance properties relative to the spray-dried SAMS Example 5 control. An application study was therefore undertaken to compare the performance of three different SAMS products in an offset type coating formulation. Specific details concerning the coating formulations and the "CLC" coating conditions are summarized in Table 6-C. The pigment portion of our coating formulations consisted of a 90/10 blend of #1 fine particle size clay/SAMS pigment wherein Samtone 581, SAMS Example 5 and the 95/5 structured pigment slurry were critically compared. The observed coating properties suggest no deleterious effects on sheet opacity as a consequence of producing a high solids slurry out of SAMS Example 5. In fact, substantial improvements in sheet gloss and printed gloss are actually provided by the slurried SAMS version relative to its original spray-dried control (compare formulation C to B) . The performance advantages are even greater when comparing (C) against the formulation containing the Samtone 581 (A) . TARTiF! 6-A Oαqariscn of Structured Pigment Slurries Produced from SftHDDNE 581 and the low Oil Absorption SAMS* SAMIENE 581/ low Oil Abs. H3-90 SAMS*/H3-90 Proper iv Composite** Composite Slurry Makedown Conditions High Shear High Shear Cowles Cowles MS/B3-90 Wt. Ratio 80/20 95/5 Slurry Solids, % 50.0 50.0 Slurry Viscosities (before Acrysol polymer stabilization): —Brookfield (20 rpm), cps 172 180 —Hercules (A-Bαb, 1100 rpm), dynes 18 + /520 rpn 18+/655 rpm Note; *SAMS product of Exaπple 5 (Table 5-A). **Rheological data and inforπation on this system taken from Example 1 (Table 1-A) of Reference 7. TABLE 6-B QpRπi ira inns for SSH5 Structured Pi tyrant Slurry Physical Property Target Value SAMSVH3-90 Ratio, by dry wt. 95/5 Slurry Solids, % 49 - 51 Waight per Gallon, lbs. 11.84 - 12.05 Acrysol ICS-1 Polymer Dosage, active wt. % (on dry pigment) 0.04 - 0.09 Brookfield Viscosity at 50% Solids, (20 rpm, #2 spindle) , cps 600 - 800 Hsrcules Viscosity at 50% Solids, (A-Bαb, 1100 rpm), dynes 18.0 - 18 + /400 rpm Particle Size (sedigraph), % - 2 microns 92-96 Wst Sieve Residue, 325 Mash (Max.), % 0.01 Note: *Iow oil absorption SAMS product.of Exaπple 5 (Table 5-A) TABLE 6-C Comparative Perf απnanoe of SAMS Pigments In an Offset Orating Application Paper Coating Formulation fin active parts) : A B C No. 1 Fine Clay (Hydragloss ) 90 90 90 SAMTONE 581 (Medium Oil Abs. SAMS Pigment)* 10 — — SAMS (frαn Exaπple 5, Table 5-A, Low Oil Abs. Pigment) — 10 — SAMS/H3-90 (95/5 SAMS/BS-90 slurry blend)** — — 10 Polyacrylate Dispersant 0.1 0.1 0.1 SBR latex (Dow 620) 10 10 10 Starch (Penford Gum 290) 4 4 4 Calcium Stearate 0.5 0.5 0.5 Note: *Pigment previously described in U.S. Patent #4,863,796; Exaπple Two. ♦♦ Composite slurry product of Table 6-B. Coating Conditions: Coating Solids = 64.5% Coat Wteight = 7.5#/Ream Basestock = 45#/Ream woodfree paper Coating Method = "CLC" pilot coater operating at 2000 fpm Super Calendered - 2 nips § 800 pli, 150°F heat Coating Properties; Property Brightness, % Gloss, % Cpacity, % Printed Gloss, % Parker Print Surf 8 5 Kgf 610 Kgf @ 20 Kgf Example 7 In this example, evaluation studies were undertaken to illustrate the titanium dioxide extension capabilities of SAMS Example 5 in some typical LWC/offset paper coating applications. Two separate coating formulations were examined, wherein both cases up to five parts of Tiθ2 pigment were successfully replaced with the SAMS product of Example 5 (see Tables 7-A and 7-B respectively) . In the first coating set, an offset formulation containing a 90/10 #1 fine particle clay/Tiθ2 pigment blend was modified such that 2.5 parts and then finally 5.0 parts of iθ2 were replaced. The SAMS product of Example 5 was added on a relative dry weight replacement basis of 3.7:1 and l.:l respectively. One hundred parts of total pigment were maintained in the formulations. Other details concerning the coating formulations or • the "CLC" coating conditions can be found in Table 7-A. As can be seen from the coating performance data of Table 7-A, the SAMS pigment allowed up to 5 parts of Tiθ2 to be removed form the formulation without any significant decrease in sheet opacity or brightness, and with a concomitant improvement in printed gloss. Sheet smoothness as measured by Parker Print .Surf was essentially equivalent to the control coating formulation. In the second offset coating study, a fine clay- carbonate type formulation was used. A 70/20/10 pigment blend of #1 fine particle size clay, ultrafine ground calcium carbonate and iθ2 pigment, respectively, was modified such that 5.0 parts of Tiθ2 was replaced with the SAMS of Example 5 at a 1.5:1 dry weight replacement ratio basis. One hundred parts of total pigment were maintained in the formulation by adjusting the fine clay content accordingly. Other details concerning the coating formulations or the "CLC" coating conditions are summarized in Table 7-B. The coating performance data of Table 7-B indicate similar performance trends as observed in the first coating set. Sheet opacity, brightness and smoothness were all maintained, while printed gloss was improved with the replacement of 5 parts Tiθ2 with 7.5 parts of SAMS Example 5. However, it should be noted that the Tiθ2 replacement efficiency of our SAMS was better in this offset formulation than in the non-carbonate containing one (1.5:1 versus 1.9:1 of SAMS to Tiθ2 respectively) . In conclusion, a unique structured pigment system has been presented that increases the amount of microvoids created in a coating formulation, which in turn increased the light scattering capacity of the coating. This enhancement in light scattering effectively allows the removal of some titanium dioxide. Up to 50% removal of Tiθ2 pigment was achieved with minimal deterioration of optical properties. The SAMS structured pigment did increase viscosity somewhat, although not excessively. ΦRPT.F 7-a T±θ2 Extension fiapiMi itiM of low Oil Absorption SAMS Pigment in a Fine Clay, Offset Grating Fαπmlatiαn Paper Coating Formulation I fin parts) : No. 1 Fine Clay (Hydragloss ) Titanium Dioxide SAMS (from Exaπple 5, Table 5-A, Low Oil Abs. Pigment) Polyacrylate Dispersant SBR Latex (Dow 620) Oxidized Corn Starch Calcium Stearate Coating Conditions: Coating Solids = 64.0% Coat Weight = 7.5#/Ream Basestock = 45#/Ream woodfree paper Coating Method = "CIC" pilot coater operating at 2500 fpm Super Calendered - 2 nips @ 800 pli, 150°F heat 03387 54 Coatin Proeri TABLE 7-B TiO 2 Extension Capabilities of low OH Absorption SAKS Pigment in a Fine Clay/Caxbonate Orating Formulation Paper Coating Formulation II fin parts): No. 1 Fine Clay (Hydragloss ) Ultrafine Ground Limestone Titanium Dioxide SAMS (frαn Exaπple 5, Table 5-A, Low Oil Abs. Pigment) Polyacrylate Dispersant SBR Latex (Dew 620) Oxidized Corn Starch Calcium Stearate Coating Conditions: Coating Solids = 65.0% Coat Weight 7.5#/Ream Basestock = 45#/Ream vroodfree paper Coating Method "CLC" pilot coater operating at 2500 fpm Super Calendered - 2 nips @ 800 pli, 150°F heat Coating Properties: Example 8 In this study, the optical performance of SAMS Example 5 was compared to that of Samtone 581 in a wet end paper f iller application . The performance properties were compared at filler loadings of 6% and 12% respectively. Details concerning the furnish and other test conditions are summarized in Table 8 . Opti cal properties including corrected opacity , brightnes s and whitenes s were determined on 5 handsheets formed for each test . The averaged results are also reported in Table 8 . TABLE 8 Comparative Performance of SAMS Pigments in a Paper Filler Application Handsheet Parameters* Pigments: A SAMTONE 581 (Example Two of U.S. Patent #4,863,796) B, Low Oil Abs. SAMS (Example 5, Table 5-A) Filler Levels: 6% and 12 % Furnish: 60% AO-2 (hardwood) and 40% International Pine (softwood) Freeness: 350 csf Basis Weight: 40#/Ream pH: To pH 4.5 with Alum Retention Aid: 0.025% Machine Calenders 2 Nips (Weight of Steel Roll only) Note: *Handsheets were formed using Tappi Method T205 om-88, rev. 1988. Results Filler Filler Bright- Whiteness Pigment Level.% ness.% Index A 6 84.5 66.8 B 6 84.5 67.5 A 12 86.2 68.9 B 12 86.3 69.1 Example 9 In this program, the optical performance properties of SAMS Example 5 were compared to those of the prior art product, Samhide 583, in an interior latex flat paint formulation. A flashed calcined clay pigment, Optiwhite, was also included in the paint study to provide a conventional control formulation for comparative purposes. A detailed outline of the test formulations is presented in Table 9. As shown there, pigments common to all three formulations included iθ2 (at 150.0 lbs./lOO gal.) and coarse ground calcium carbonate (at 123.0 lbs./lOO gal.). The pigment volume concentration of these formulations was 58.9%. The SAMS test pigments in this paint study were used in combination with a high brightness, fine particle size hydrous caly (Huber HG-90). In both cases, a 55/45 dry weight ratio of HG-90/SAMS was employed to yield composite pigment systems. The HG- 90j/SAMS composites were then compared head to head with Optiwhite calcined clay on an equal volume replacement basis to keep the PVC constant. The paint properties for these formulations are presented in table 9. Paint B, which contains the SAMS of Example 5, showed some significant performance advantages in hiding power (i.e., contract ratio) and in relative tinting strength versus Paint A containing Samhide 583. When compared to the Optiwhite control formulation, the relative optical advantages seen with SAMS Example 5 are even greater. In terms of sheen and gloss. Paint B yielded somewhat higher values than the other formulations. This property can be attributed to the fine particle size nature of our SAMS Example 5 and Huber HG-90 products. This performance feature can be considered an advantage from the standpoint that it provides greater formulation flexibility. Latex paint formulations ranging from flats to satin finishes can thus utilize SAMS Example 5, whereas Samhide 583 often provides too much flatting efficiency to be used in the latter. TABLE 9 Comparative Performance of SAMS Pigments In an Interior, Latex Flat Paint Application 1. Interior Latex Flat Formulation ibs, er 100 allons ; Example 10 In this study, a low oil absorption SAMS pigment in accordance with our invention (reaction product #1 of Table 4-A) was examined as a high brightness rein- forcing filler in a white rubber formulation. The rubber formulation used in this study is typical of those for a white sidewall tire application. Specific details concerning the components of our screening formulation can be found in Table 10-B. The SAMS product of this invention was examined as originally produced (per Example 4) and in a pH adjust¬ ed form. The latter product was produced by adding sufficient sulfuric acid to the SAMS dispersed filter cake material to obtain a slurry pH of 6.2 and then spray-drying as before. Fillers used as controls in our rubber study included Samflex 585 (per the prior SAMS art) and Nucap 100W (a high brightness, fine particle size, Mercaptosilane-modified kaolin clay) . All SAMS materials were used without the addition of any Mercaptosile treatment. The comparative physical properties of the various test fillers are summarized in Table 10-A. In Table 10-B, the physical testing results from our study are summarized. The test data indicate that the new SAMS of pH 6.2 provided reinforcement proper¬ ties virtually equivalent to that of Nucap 100W. It is truly remarkable that an untreated clay based product would provide modulus and tear properties equal to that of a Mercapto-treated clay. In comparison to Samflex 585 of the prior art, the new SAMS of pH 6i.2 offered far superior modulus and tear properties. the pH adjustment of our low oil absorption SAMS (compare formulations B and C) was seen to desirably lengthen the cure time plus improve modulus and tear properties. However, modulus and tear were gained at the expense of some tensile and elongation. Of particular note was the superior optical performance of the new SAMS prod¬ ucts (original or pH adjusted) versus the other fill- ers. It is also truly remarkable that SAMS fillers of lower starting brightness should so clearly out perform Samflex 585 in rubber compound brightness and whiteness values. This performance feature can be explained on the basis of superior capabilities in Tiθ2 extension. In summary, the excellent reinforcement and opti¬ cal performance properties of SAMS products from this invention, make these materials highly desirable fill¬ ers for white rubber formulations. In addition, the greater reinforcement properties of our new SAMS are unexpected given the prior art concepts of structure/ performance based on oil absorption. TABLE 10 -A SAMS Products Used as Fillers in a White Sldewall Rubber Compound Test Compounds Filler Portion A SAMFLEX 585 (Medium Oil Abs. SAMS; per Example Two of U.S. Patent #4,863,796) B Low Oil Abs. SAMS (Rxn Product #1, Table 4-A) Low Oil Abs. SAMS pH adjusted to 6.2 (per this Example) D Nucap 100W (Mercapto-treated, high brightness kaolin clay filler) Filler - Physical Properties Bright- Particle Oil pH ness. Size, Abs., (810% Specific % % - 2m g/lOQg solids) Gravity SAMFLEX 585 92.6 60 150 10.8 2.43 Low Oil Abs. SAMS 91.8 87 108 10.6 2.52 Low Oil Abs. SAMS (pHadj.) 91.8 87 108 6.2 2.52 Nucap 100W 88.0 95 40 6.3 2.60 ______________ Cαπparative Performance of SAMS Fillers in a White Sidffwnn Rubber Compound Rubber Formulation Test Cαr ounds*** Note: *Ccπpαnent levels are specified in terms of parts per hundred rubber (phr). ★★ Filler levels were adjusted in order to πeintain a constant specific gravity in the final rubber formulation. ***See Table 10-A fo Physical Testing Results ProperLy Rheometer (T=90%, min.) Durometer (A), pts. Tensile, psi Elongation, % Modulus 8100% E, psi Modulus 8 200% E, psi Modulus 8300% E, psi Tear Die "C", pli Specific Gravity +0.02 Compound Brightness, % Ccπpound Whiteness, W.I. 77.0 81.0 80.7 75.7

Claims: Claims 1. A sodium aluminosilicate pigment having the following empirical formula in terms of oxide con¬ stituents: (0.01-0.5) Na2θ : I2O3 : (2.01-3.0) Siθ2 : (1.0-3.0) H 2 0, said pigment being produced by the hydrothermal reaction of a sodium silicate and a clay in an aqueous medium at a ratio of sodium silicate (B) to clay (C) of 0.1:1 to 0.5:1, said pigment being characterized by having a pore volume structure of at least 2.0 ml/gm, a relatively narrow pore size distribution, an oil absorption of less than about 115 gm/100 gm and an average particle diameter of 0.5-0.7, as determined by x-ray serigraph, said hydrothermal reaction being carried out using a carefully controlled combination of reaction conditions including a batch reaction mixture comprising: (0.2-0.5) Na2θ : AI2O3 : (2.30-2.83) Siθ2- 2. A sodium aluminosilicate pigment according to claim 1 wherein the Siθ2/ a2θ mole ratio in the batch reaction ranges from 0.1:1 to 3.33:1, and pore volume exceeds 2.5 ml/gm. 3. A sodium aluminosilicate pigment according to claim 2 wherein, in the reaction, the silicate used is a high mole ratio silicate and the B/C molar ratio ranges from 0.2 to 0.3. 4. A sodium aluminosilicate pigment according to claim 2 wherein the ratio of B/C is from 0.3-0.5 and the Siθ2/Na2θ mole ratio of the starting silicat.e ranges from 1.0-1.9, and the oil absorption value ranges from 30 gm/100 gm to 115/100 gm. 5. A method for the production of a sodium alumi¬ nosilicate pigment which comprises the reaction of a sodium silicate having a Siθ2/Na2θ mole ratio of 1.0 to 3.33 with clay under hydrothermal reaction conditions at a mole ratio of sodium silicate (B) to clay (C) of 0.1 to 0.5, the reaction being carried out using the following batch reaction mixture: (0.2-0.5) a2θ : I2O3 : (2.30-2.83) Siθ2- 6. A method according to claim 5 wherein during the reaction, the reaction solids range from 10 to 14 wt.%. 7. A method according to claim 5 wherein the reaction is carried out by adding sufficient steam to the reactor to establish thermal reaction conditions ranging over a period of 10 minutes to 45 minutes under a steam pressure sufficient to raise the reactor pressure to 55 psi. 8. A method according to claim 5 wherein the Siθ2/Na2θ mole ratio in the batch reaction ranges from 0.1:1 to 3.33:1,. respectively. 9. A composite product comprising structured agglomerants produced by the reaction of sodium silicate (B) and kaolin clay (C) under hydrothermal conditions at a B/C ratio of 0.1:1 to 0.5:1; said structured agglomerants being characterized by having (a) a total pore size of greater than 2.0 ml/gm, which represents the sum of the microvoids within the structured agglomerants; (b) a pore volume consisting of microvoids within said structured agglomerants which have a pore diameter size of 0.2 to 0.7 microns, said pore diameter size being near the optimal porosity for the efficient scattering of light for a porous material having a refracting index of 1.5; (c) an oil absorption of less than 115 gm/100 gm; and (d) an agglomerated particle size of about 0.5 to 0.7 microns with 86% of the particles being less than 2 microns. 10. A method for the preparation of sodium alumin¬ osilicate pigments which have a pore size distribution centered near the optimal porosity design of 0.3 micron for efficient scattering of visible light, which comprises: (a) selecting kaolin clay reactants which have an average ultimate particle size of about 0.2 to 0.6 micron based on serigraph measurements; (b) providing a sodium silicate solution which has an Siθ2/Na2θ mole ratio of about 1.0:1 to 3.33:1; (c) mixing the. kaolin clay with the sodium silicate solution in an aqueous medium at a ratio of sodium silicate (B) to kaolin clay (C) of 0.1:1 to 0.5:1, and at a batch reaction mixture comprising (0.2-0.5) Na2θ : AI2O3 : (2.30-2.83) Siθ2,* (d) reacting said mixture under hydrothermal conditions by heating in the presence of steam to a pressure in the range of 100 to 150 psig and a tempera- ture of up to 175°C; (e) continuing said reaction for a sufficient period for the sodium silicate to react with kaolin clay and form structured agglomerants composed of aggl¬ omerated small flat platelets, wherein the platelets have an integrated rimmed area of amorphous non- diffracting sodium silicate clay reaction product and the primary particles are generally in the form of irregular to pseudo-hexagonal shaped plates, said structured agglomerants being characterized by the following properties: (1) an oil absorption of less than 115 gm/100 gm; (2) an agglomerated particle size of about 0.5-0.7 micron with 85% of the particles being less than 2 microns; (3) a total pore volume of greater than 2.0 ml/gm; and (4) a pore volume consisting of microvoids within said structured agglomerants, which microvoids have a pore diameter of 0.2 to 0.7 microns; wherein said total pore volume (3) represents substan¬ tially the sum of the microvoids contained within said structured agglomerants. 11. A method for the preparation of pigments which have a pore volume as represented by the sum of the microvoids which have void diameters as measured in microns which are comparable in size to the optimal wavelength range for efficient scattering of visible light, which comprises: (a) determining the optimal scattering efficiency of a porous clay medium having a predeter¬ mined refractive index; (b) selecting a clay starting material of said predetermined refractive index which has an average ultimate particle size in microns which is comparable to the micron size of the microvoids necessary for the optimal wavelength range for effi- cient scattering of visible light; (c) reacting a sodium silicate solution (B) with said clay (C) in aqueous medium under hydrothermal conditions to produce an- agglomerated reaction product; and (d) recovering said agglomerated reaction product, said agglomerated product being composed of agglomerated small flat platelets, said agglomerated products having an agglomerate particle size comparable in size to the clay starting material, and a total pore volume as represented by the sum of the microvoids between the particles in said agglomerate, which is comparable to the pore volume of a pigment which has the optimal wavelength range for efficient scattering of visible light. 12. A paper composition containing as a pigment or filler the sodium aluminosilicate pigment of claim 1. 13. A paint composition containing as a paint pigment, the sodium aluminosilicate pigment of claim 1. 14. A rubber composition containing as a reinforc¬ ing pigment, the sodium aluminosilicate pigment of claim 1.

Inventors: FREEMAN GARY M, FREEMAN, GARY, M.
Applicants: HUBER CORP J M, J.M. HUBER CORPORATION
Application year: 1991
Main classification: C09C1
IPC codes: C01B33, C04B28, C08K3, C08K5, C08L21, C09C1, C09D7, D21H17, D21H19