ACTIVATED CLAY COMPOSITION AND METHOD

Abstract: High performance acid activated clays suitable for bleaching oil are produced by contacting an intercalating clay mineral with a strong acid in a polar organic liquid.

Description: ACTIVATED CLAY COMPOSITION AND METHOD Technical Field This invention relates to clay-based compositions suitable for the bleaching of oil. In particular, the present invention is directed to oil bleaching compositions treated with a polar organic compound and an acid. Background of the Invention Fats and fatty oils, commonly called triglycerides, are constituted of triesters of glycerol, and include minor amounts of fatty acids. At ambient temperatures, about 20° to about 25°C, fats are solids, whereas fatty oils are liquids. Triglycerides are widely distributed in nature. Some triglycerides are edible while others are not. Many are derived directly from vegetable, animal, and marine sources. Others are obtained, as by¬ products, in the production of fiber from vegetable matter, and in the production of protein from vegetable, animal or marine matter. Edible vegetable oils include canola, coconut, corn germ, cottonseed, olive, palm, peanut, rapeseed, safflower, sesame seed, soybean, and sunflower oils. Examples of nonedible vegetable oils are jojoba oil, linseed oil and castor oil. Illustrative sources of edible animal-derived oil include lard and tallow. Examples of nonedible animal-derived oil are low grade tallow and neat's-foot oils. Some of these oils may have the color that is objectionable to a consumer. Thus, the oil needs to be bleached to improve its color quality. To this end, a great many oils are commonly treated with bleaching clays to reduce oil color values by adsorptive purification. Bleaching clays generally improve oil color quality by adsorbing color impurities that are present. Color impurities typically present in oils include, for example, carotenoids, xanthophylls, xanthophyll esters, chlorophyll, tocopherols, as wel oxidized fatty acids and fatty acid polymers. It is also desirable to remove color impurities from a nonedible oil to obtain a desirabl color. Natural clays, e.g., Fuller's earth and th bentonites, have commonly been used as bleaching cla to remove both the naturally-occurring and the otherwise-present, e.g., the thermally-induced, colo impurities from edible and nonedible oils. It has b suggested that clays containing a zeolite can be use for such a purpose as well. Acid-activated clays have also been used f this purpose. Such clays generally remove a relativ wider spectrum of color impurities. A conventional process for producing acid-activated bleaching clays utilizes calcium bentonite clays and sulfuric acid. The calcium bentonites used in the acid activation process typic are neutral to mildly basic. The acidic salts forme during activation and residual acid can be washed of and separated by filtration from the product clay, i desired. However it is not necessary to do so. Another type of naturally-occurring clay, frequently classified as palygorskite clays, require heat to impart bleaching activity. Mineralogically, palygorskite clays are distinguishable from the bentonites (smectites or montmorillonites) . Summary of the Invention Highly active clay-derived bleaching compositions are obtained by acid activation of an intercalating clay mineral in the presence of a polar organic liquid such as an aliphatic C x to C 6 monohydric alcohol or an aliphatic C 2 to C 6 aliphatic ether. Acid activation with an inorganic acid or with an organic acid in this manner can be effected at ambient temperatures, and in a relatively short time period of the order of minutes. After acid activation, the obtained product is air dried, size reduced and classified if desired, and is then ready for use. Description of the Embodiments While this invention is susceptible to embodiments in many different forms, preferred embodiments of the invention are described below. It should be understood, however, that the present disclosure is to be considered as a exemplification of the principles of the invention and is not intended to limit the invention to the specific embodiments illustrated. The compositions of the present invention are acid activated clay intercalates and are useful for reducing the amount of color impurities in an oil. Throughout this application, the term "oil," and the grammatical variations thereof, includes vegetable-derived, animal-derived as well as marine source-derived fats and fatty oils that are liquids at the particular temperature that is necessary for desired processing of a particular type of oil. In use, the oil and the present oil bleaching composition are combined in a suitable vessel to produce a slurry. The resulting slurry is maintained at an elevated temperature and at a pressure no greater than about atmospheric pressure for a time period sufficient to reduce the amount of color impurities of the oil without causing degradation of the oil, i.e., the oil is bleached substantially without thermal decomposition of the oil. A bleached oil is then recovered from the slurry. The bleaching is performed at a temperature elevated above room temperature, i.e., at about 30°C higher, but below the temperature that induces therma decomposition of the oil. A preferred bleaching temperature is in a range of about 50° to about 130°C more preferably about 60° to about 125°C. The pressure at which the bleaching is performed can be atmospheric or less than atmospheric (subatmospheric) , as desired. A preferred reduced pressure is in a range of about 1 to about 5 inches o mercury. A most preferred reduced pressure is about inches of mercury. The time period sufficient to reduce the amount of color impurities in the oil utilizing the present bleaching compositions usually is in a range about 5 to about 90 minutes. Oils that can be bleached using the composition of the present invention include both edi and inedible oils. Illustrative oils are those previously mentioned hereinabove. Clays suitable for the activating treatment the present invention are intercalating clays, i.e., those clays that admit organic compounds of polar or ionic character into channels formed by the arrangeme of octahedral units and tetrahedral units or between stacked layers formed by an octahedral sheet and one more tetrahedral sheets of the atoms that constitute clay mineral structure. Illustrative are the natural occurring clay minerals of the hormite group such as palygorskites and the sepiolites, which define channe formed by octahedral units and tetrahedral units of t clay mineral structure, and the bentonites (mont orillonites and smectites) , which are constitut by stacked layers formed by an octahedral sheet and one or more tetrahedral sheets, and mixtures of the foregoing. Previously acid activated bleaching clays, such as those commercially available, e.g., FILTROL ® 105 SF, PURE-FLO ® Supreme, and the like, are also suitable. As to the latter grouping of clay minerals, the bleaching activity of these acid activated bleaching clays (usually acid-treated calcium bentonites) can be further enhanced by the treatment provided by the process of the present invention. Clay minerals preferred as starting materials for making the present compositions are neutral clays that already exhibit some bleaching activity. These clays have a pH value in the range of about 7 to about 9. The pH value of the clay is determined from a 5-weight percent slurry of the clay in distilled water; the slurry is agitated for three minutes prior to measurement of the pH value by a conventional pH meter. Palygorskite (attapulgite) - and smectite-containing neutral bleaching clays are particularly preferred as starting materials for the present purposes. Palygorskite (attapulgite) , a mineral found in some clays, is a hydrous silicate material represented by the approximate formula: (OH 2 ) « (OH) 2 Mg 5 Si 8 O 20 *4H 2 O. See, e.g., Grim, R.E., Clay Mineralogy, 2nd ed., McGraw-Hill, Inc., New York, N.Y. (1968), p. 115. Smectite is a generic term that refers to a variety of related minerals also found in some clays. The smectite minerals typically occur only as extremely small particles. Generally, smectite is believed to be composed of units made of two silica tetrahedral sheets with a central alumina octahedral sheet. Each of the tetrahedra has a tip that points to the center of th smectite unit. The tetrahedral and octahedral sheets are combined so that the tips of the tetrahedra of e silica sheet and one of the hydroxyl layers of the octahedral sheet form a common layer. See Id. , pp. 7 78. In particular, the smectite family of clays includes the various mineral species montmorillonite, nontronite, hectorite and saponite, all of which can present in clay in varying amounts. Other minerals, neither of the smectite gen nor of the palygorskite variety, that can be present clay include apatite, calcite, the feldspars, kaolini mica, quartz and sepiolite. A polar organic liquid suitable for practic the present invention is one the molecules of which penetrate between the clay mineral layers or into the defined channels of the clay mineral and can displace interlayer water molecules that are present. Prefera the Polarity Index (P.I.) of such liquids is greater than about 1.5 but less than that of water. The term "Polarity Index" as used herein an in the appended claims is determined according to Snyder, J. Chromatographic Science 16..-223-234 (1978) . Polar organic liquids well suited for the present purposes are the C to C 6 aliphatic monohydric alcohols, e.g., methanol (P.I.=5.1), ethanol (P.I.=4. isopropanol (P.I.=3.9), n-propanol (P.I.=4.0), n-buta (P.I.=3.9), isobutanol (P.I.=3.9), t-butanol (P.I.=4. isopentanol (P.I.=3.7), n-hexanol, mixtures thereof, the like, and the C 2 to C 6 aliphatic ethers, e.g., dimethyl ether, diethyl ether (P.I.=2.8), methyl ethy ether, diisopropyl ether (P.I.=2.4), n-butyl ether (P.I.=2.1), mixtures thereof, and the like. The polar organic liquid may be used alone or in an admixture with a non-polar organic liquid such as a liquid aliphatic hydrocarbon, e.g., hexane or heptane. The volume ratio for the admixtures of a polar liquid with a non-polar liquid can vary over a relatively wide range as long as a sufficient amount of the polar liquid is present to effect the desired degree of activation. From a processing perspective, it is preferable to utilize azeotropic admixtures inasmuch as the admixture recovered upon drying can be readily recycled and reused. To that end, particularly preferred are the ethanol/n-heptane binary azeotrope boiling at about 72°C (760 mm Hg) and constituted by about 67 mole-% ethanol and 33 mole-% n-heptane, and the ethanol/n-hexane binary azeotrope boiling at about 59°C (760 mm Hg) and constituted by about 33.2 mole-% ethanol and about 66.8 mole-% n-hexane. For acid activation of the intercalating clay mineral the acid can be inorganic or organic having a pKa value not greater than about 7. Mineral acids such as hydrochloric acid, phosphoric acid or sulfuric acid are preferred. Particularly preferred is sulfuric acid in a relatively high concentration. Also suitable are strong organic acids such as formic acid (HCOOH; pKa=3.75), acetic acid (CH 3 COOH; pKa=4.76), oxalic acid (H00CC00H; pKa=1.25 and 4.14), citric acid (pKa=3.14, 4.77 and 6.39) and the like. The intercalating clay mineral to be acid activated in accordance with the present invention can be wet or dry, as desired. That is, the clay mineral can contain as much as about 55 weight percent free moisture, preferably no more than about 50 weight percent free moisture. The clay mineral is combined with an acid/polar liquid admixture so as to form a slurry which is then agitated for a relatively brief time period in the range of about 1 to about 3 minut Thereafter the slurry is filtered to remove the pola organic liquid and air dried, usually at about ambie temperature, to a volatile matter content of no more than about 35 weight percent, preferably about 20 we percent, more preferably about 10 weight percent, ba on the weight of the clay mineral, to produce a bleaching clay product that exhibits enhanced bleach activity. The produced bleaching clay product can b used as is, or it can be subjected to a size reducti procedure, e.g., pulverization, prior to packaging a use. For bleaching an oil, the amount of the present bleaching clay that is combined with the oil be bleached usually is in the range of about 1 to ab 5 weight percent, based on the weight of the oil. Lesser or larger amounts can be used, depending upon oil to be treated and the severity of the desired bleaching treatment. The acid activation process embodying the present invention can be carried out batchwise, or as continuous process, as convenient. The continuous activation process can be a countercurrent process o co-current process. The agitation of the clay/acid/polar liquid slurry during the activation process can be readily achieved by the use of a stati mixer, a commercially available blender, or the like expedient. The present invention is illustrated by the following examples. In these examples the red color the treated oil was monitored in accordance with American Oil Chemists Society (AOCS) Official Method CC13b-45, and light absorption at 450 nanometers (nm) EXAMPLE 1: Acid Activation Using Ethanolic Sulfuric Acid Attapulgite-smectite clay was pre-treated with concentrated aqueous sulfuric acid (18M; 3 wt.-% H 2 S0 4 ) . Aliquots of this pre-treated clay were combined with sulfuric acid in 95% ethanol (224 grams of clay at —47 wt.-% free moisture with 1000 ml of 0.03M H 2 S0 4 in ethanol and 256 grams of clay at —47 wt.-% free moisture with 1000 ml of 0.15M H 2 S0 4 in ethanol). The resulting slurries were stirred for about 30 minutes at ambient temperature (about 25°C) , filtered using a Buchner filter, and air dried at ambient temperature to a volatile matter content of less than about 20 weight percent. The air dried products were then pulverized to a mean particle size of about 25 to 30 microns and used to bleach corn oil with 3 wt.-% dose of the clay for about 30 minutes. The observed results are presented in Table I, below. TABLE I Bleaching Performance Red Color Absorbanc Bleaching Clay Value @ 450 n None 8.1 1.885 Commercial Product 1 1.5 0.171 A/S 2 (3 wt.-% H 2 SO 4 ) 2.5 0.261 A/S 2 (3 wt.-% H 2 SO 4 ) 2.5 0.265 A/S 2 (3 wt.-% H 2 SO 4 ) 2.5 0.236 A/S 2 (0.03M H 2 SO 4 /EtOH/30 min.) 2.0 0.215 A/S 2 (0.15M H 2 SO 4 /EtOH/30 min.) 1.6 0.186 A/S 2 (0.15M H 2 SO 4 /EtOH/30 min.) 1.3 0.131 A S 2 (0.3M H 2 SO 4 EtOH/30 min.) 1.0 0.124 A/S 2 (0.15M H 2 SO 4 /EtOH/10 min.) 1.1 0.150 A/S 2 (0.3M H 2 SO 4 /EtOH/10 min.) 1.2 0.142 A/S 2 (3 wt.-%H 2 SO 4 ;EtOH/H 2 O/30 min.) 2.4 0.259 A/S 2 (3 wt.-%H 2 SO 4 ;EtOH/H 2 O/60 min.) 2.1 0.247 1 FILTROL® 105 SF, available from Engelhard Corporation. Attapulgite-smectite mixture. The data presented in Table I, above, clea demonstrate the enhanced bleaching activity of clays treated with ethanolic sulfuric acid as compared to t same clay acid-activated using 3 weight percent sulf acid in conventional manner with or without a follow- treatment only with ethanol/water mixtures. EXAMPLE 2: Acid Activation of Various Clays With Ethanolic Sulfonic Acid Clays from various sources were combined with sulfuric acid in 95% ethanol (250 grams of clay at -47 wt.-% free moisture with 1000 ml of 0.15M H 2 S0 4 in 95% ethanol) . The slurries thus produced were stirred for about 5 minutes at ambient temperature (about 25°C) , filtered, and air dried at ambient temperature to a volatile matter content of about 10 weight percent. The air dried products were then pulverized (80% through 325 mesh, U.S. Sieve Series) and used to bleach corn oil for 30 minutes at a 3 wt.-% dose. The observed results are presented in Table II, below. TABLE II Corn Oil Bleached With Various Clavs Red Color Absorbance Bleaching Clay Value @ 450 nm None 8.1 1.885 THOMAS COUNTY, GA CLAY, AREA 1 ' base clay 2.1 0.247 treated clay 1.7 0.203 % improvement 20 THOMAS COUNTY, GA CLAY, AREA 2 1 base clay 2.3 0.233 treated clay 1.6 0.167 % improvement 30 THOMAS COUNTY, GA CLAY, AREA 3 1 base clay 2.2 0.233 treated clay 1.5 0.173 % improvement 32 TIPPAH COUNTY, MS CLAY 2 base clay 2.8 0.286 treated clay 2.3 0.228 % improvement 18 1 palygorskite-smectite mixture 2 smectite-opal mixture EXAMPLE 3: Acid Activation of Clay With Polar Liquids Clay aliquots from Thomas County, GA, Area mine (palygorskite/smectite; 250 g, ~47 wt.-% free moisture, through 3/16-inch screen) were treated with sulfuric acid dispersed in various polar liquids. T treatment was performed as in Example 2 but with the indicated solvent in place of ethanol. Activated clay products obtained in the foregoing manner were tested by bleaching corn oil exhibiting a Red Color Value of about 8.1 and Absorbance ©450 nm of about 1.885. The bleaching was performed at a 3 weight percent dosage for a time period of 30 minutes. The observed results are presented in Table III, below. TABLE III Bleaching Efficacv Polarity Red Color Absorbance Polar Liquid Treatment Index Value @ 450 nm ethanol 5.2 1.1 0.135 iso-propyl alcohol 4.3 1.1 0.143 methyl alcohol 6.6 1.3 0.154 hexane 0.0 2.1 0.211 ethyl ether 2.9 1.5 0.165 water 9.0 2.7 0.195 1,2-propanediol, 99%' 3.6 0.352 1,2-propanediol, 99% 2 3.2 0.292 hexane/iso-propyl alcohol 1.6 0.224 (vol. ratio 1:1) heptane/ethanol 1.5 0.203 (vol. ratio 7:3) 1 16.6% Free Volatiles. 2 1.2% Free Volatiles. EXAMPLE 4: Duration ofActivation Treatment Clay aliquots from a Georgia mine of Oil-D Corporation of America (palygorskite/smectite; 250 g, -47 wt.-% free moisture, through 3/16-inch screen) treated with 1000 milliliters of 0.3 M sulfuric acid 95% ethanol in a manner similar to Example 1, above, were used to bleach corn oil for 30 minutes. The am of clay was about 3 weight percent, based on the wei of oil . The observed results are presented in Table below. TABLE IV Effect of Activation Duration Activation Time, Red Color Absorbanc Bleaching Clay min. Value @ 450 nm Palygorskite/Smectite 10 1.0 0.132 Palygorskite/Smectite 5 1.2 0.154 Palygorskite/Smectite 0.25 1.1 0.144 None N/A 8.1 1.885 Data in the foregoing Table indicate that t activation process is virtually instantaneous when t acid activated bleaching clays of the present inventi are utilized. EXAMPLE 5: Performance Enhancement ofCommercially Available Bleaching Clays The procedure typically used to treat raw c was modified to compensate for the difference in per free moisture between the raw clays (47% free moistu and the commercial products (10-15% free moisture) . modification involves adding water to the clay/ethan slurry to bring the total water in the system to similar levels as found in the process using raw clay. The ratios of dry weight clay to total weight of water and total volume of acidified ethanol were held constant. Comparison ofProcedures: RAW CLAY METHOD: — 250 g raw clay (47% free moisture) — 1000 ml acidified ethanol (50 ml 3.3 M H 2 SO 4 in 1000 ml ethanol) — 5 minutes slurry time — Filtered, dried and pulverized — Clay (dry weight) to ethanol (volume) ratio: 0.13 — Clay (dry weight) to water (weight) ratio: 0.47 COMMERCIAL CLAY METHOD: — 36.25 g processed clay (10-15% free moisture) — 27.5 g water — 250 mL acidified ethanol (50 mL 3.3.M H 2 SO 4 in 1000 ml ethanol) — 5 minutes slurry time — Filtered, dried and pulverized — Clay (dry weight) to ethanol (volume) ratio: 0.13 — Clay (dry weight) to water (weight) ratio: 0.50 The treated clays were then used at various dosages to bleach canola oil and corn oil. The corn oil was bleached at 220°F . (104°C) for 30 minutes under 25 inches Hg vacuum, and the canola oil was bleached at 230°F (110°C) for 30 minutes under 25 inches Hg vacuum. The observed results are presented in Tables V-VII, below. TABLE V Corn Oil Bleaches (3 wt.-% Clav) Absorbance Percent Percen Clay Red 450 nm Improvement Improve Color 1 cm cell Red Color Absorba Optimum FF 2.8 0.290 Treated Optimum FF Lo 2.8 0.297 0.00% -2.41% Tonsil Supreme 2.7. 3.0 0.263, .281 Treated Tonsil Supreme Lo 2.4, 2.5 0.224, .235 14.04% 15.62 Acticil 3.1 0.303 1 0 Treated Acticil Lo 2.8 0.295 9.68% 2.64% Filtrol 105 SF 2.5 0.248 Treated Filtrol 105 SF Lo 1.9 0.191 24.00% 22.98% Filtrol 160 2.5 0.228 Treated Filtrol 160 Lo 2.0 0.174 20.00% 23.68% 15 Fulmont Premiere 2.9. 2.8 0.265, .278 Treated Fulmont Premiere Lo 2.7, 3.1 0.250, .274 -1.75% 3.50% Fulmont AA 3.1 0.300 Treated Fulmont AA Lo 2.8 0.264 9.68% 12.00% Gallion V2 2.4 0.229 20 Treated Gallion V2 Lo 2 0.173 16.67% 24.45% Gallion VI 2.8 0.264 Treated Gallion VI Lo 2.9 0.260 -3.57% 1.52% Clarion 470 2.5, 3.1 0.271, .273 Treated Clarion 470 Lo 2.3, 2.7 0.229, .239 10.71% 13.97% 25 Clarion 212 2.9, 3.0 0.263, .277 Treated Clarion 212 Lo 2.9, 2.8 0.254, .225 3.39% 1 1.30% Sienna Indonesia 2.5, 2.7 0.256, .266 Treated Sienna Indonesia Lo 2.5, 2.8 0.244, .257 1.92% 4.02% Pure-Flo B80 3.3 0.313 30 Treated Pure-Flo B80 Lo 3.3 0.340 0.00% -8.63% Pure-Flo Supreme 3.3 0.323 Treated Pure-Flo Supreme Lo 2.9 0.271 12.12% 16.10% RAW (12% FM) 2 3 0.295 Treated Lo 2.4 0.235 20.00% 20.34% 35 Treated Hi 1 2.2 0.228 26.67% 22.71% Starting Oil 7.7 1.673 N/A N/A 1 Lo and Hi denote acid strength of acidified ethanol (.15M and .30M, respectively) 2 Thomas County, GA clays, Area 2 40 No. of Samples 14 14 Avg. Improvement 9.13% 10.74% Std Deviation 8.79% 10.21% TABLE VI Canola Oil Bleaches (1.5 wt.-% Clay) Absorbance Percent Percent Percent Red Color 450 nm Chlorophyll Improvement Improvement Improvement Clay 1" Path 1 cm Cell PPB Red Color Absorbance Chlorophyll Pure-Flo Supreme 1.4 0.687 1009 Treated Pure-Flo Supreme Lo' I . I 0.543 576 21% 21% 43% Treated Pure-Flo Supreme Hi 1 1.1 0.620 586 21% 10% 42% Filtrol 105 SF 1.4 0.738 1 142 Treated Filtrol 105 SF Lo I.I 0.591 659 21% 20% 42% Fulmont Premiere 1.7 1.209 1540 I Treated Fulmont Premiere Lo 1.3 0.664 979 24% 45% 36% Tonsil Supreme 1.4 0.64 802 Treated Tonsil Supreme Lo 1.3 0.638 669 7% 0% 17% Gallion V2 0.8 0.435 374 Treated Gallion V2 Lo 0.9 0.454 276 -12.5% -4% 26% Starting Oil >20 N/A 26,000 Lo and Hi denote acid strength of acidified ethanol (.I5M and .30M, respectively) TABLE VII Canola Oil Bleaches (3 wt.-% Clay) Absorbance Percent Percent Percent Clay Red 450 nm Chlorophyll Improvement Improvement Improvement Color 10 cm Cell PPB Red Color Absorbance Chlorophyll Pure-Flo Supreme 2.5 2.39 97 Treated Pure-Flo Supreme Lo 1 1.7, 1.8 1.799, 1.91 1 50, 55 30% 22% 46% Treated Pure-Flo Supreme Hi' 1.6, 1.6 1.594, 1.695 29, 34 36% 31% 32% Filtrol 105 SF 1.7 1.986 216 Treated Filtrol 105 SF Lo 1.2 1.607 120 29% 1 % 44% Fulmont Premiere 2.2 2.729 393 α> Treated Fulmont Premiere Lo 1.7 1.753 97 23% 36% 75% I Tonsil Supreme 1.9 2.004 129 Treated Tonsil Supreme Lo 1.5, 1.3 1.691, 1.667 164, 163 26% 16% -27% Gallion V2 1 1.493 92 Treated Gallion V2 Lo 0.9 1.063 75 10% 29% 18% Starting Oil >20 N/A 26,000 Lo and Hi denote acid strength of acidified ethanol ( I 5M and .30M, respectively) In Tables VI and VII above, canola oil colors were read with a one inch path for the bleached oil samples treated with 1.5 wt.-% clay and a 5.25 inch path for the bleached oil samples treated with 3.0 wt.-% clay. Canola oil absorbance readings were read with a one cm cell for the bleached oil samples treated with 1.5 wt.-% clay and a 10 cm cell for the bleached oil samples treated with 3.0 wt.-% clay. This invention has been described in terms of specific embodiments set forth in detail. It should be understood, however, that these embodiments are presented by way of illustration only, and that the invention is not necessarily limited thereto. Modifications and variations within the spirit and scope of the claims that follow will be readily apparent from this disclosure, as those skilled in the art will appreciate. For example, the present method can be practiced as a batch process or as a continuous process, as desired. For a continuous process, a countercurrent flow of particulate clay and the acid-bearing polar liquid is preferred.

Claims: WE CLAIM: 1. A method for producing a bleaching cl which comprises selecting an intercalating clay mine having a structure capable of receiving a polar orga liquid, combining the selected clay mineral with an admixture of an acid and a polar organic liquid havi polarity index greater than about 1.5 but less than of water to produce a slurry, and thereafter recover a bleaching clay from said slurry. 2. The method in accordance with claim 1 wherein the acid is an inorganic acid. 3. The method in accordance with claim 2 wherein the inorganic acid is sulfuric acid. 4. The method in accordance with claim 1 wherein the acid is an organic acid having a pKa val not greater than about 7. 5. The method in accordance with claim 4 wherein the organic acid is citric acid. 6. The method in accordance with claim 1 wherein the polar liquid is an aliphatic C α to C 6 monohydric alcohol. 7. The method in accordance with claim 6 wherein the alcohol is ethyl alcohol. 8. The method in accordance with claim 6 wherein the alcohol is isopropyl alcohol. 9. The method in accordance with claim 6 wherein the alcohol is methyl alcohol. 10. The method in accordance with claim 1 wherein the polar liquid is an aliphatic C 2 to C 6 eth 11. The method in accordance with claim 1 wherein the ether is ethyl ether. 12. A bleaching clay produced in accordan with the method of claim 1. 13. A method for producing a bleaching cl which comprises combining an intercalating clay mine having a structure capable of receiving a polar organic liquid, with an acid and with a polar organic liquid which is a member of the group consisting of an aliphatic C : to C 6 monohydric alcohol and an aliphatic C 2 to C 6 ether. 14. The method in accordance with claim 13 wherein the clay is an attapulgite-smectite mixture. 15. The method in accordance with claim 13 wherein the clay is a palygorskite-smectite mixture. 16. The method in accordance with claim 13 wherein the clay is a smectite-opal mixture. 17. The method in accordance with claim 13 wherein said polar liquid combined with the clay is an aliphatic C x to C 6 monohydric alcohol. 18. The method in accordance with claim 17 wherein said aliphatic alcohol is ethanol. 19. The method in accordance with claim 18 wherein said acid is sulfuric acid. 20. A method for producing a bleaching clay which comprises combining a palygorskite-smectite mixture with ethanol and sulfuric acid to produce a slurry and thereafter drying the slurry to a volatile matter content of no more than about 35 weight percent. 21. The method of claim 20 wherein the produced slurry is dried to a volatile matter content of no more than about 20 weight percent. 22. The method of claim 20 wherein the produced slurry is dried to a volatile matter content of no more than about 10 weight percent. 23. A method for producing a bleaching clay which comprises combining an intercalating clay mineral, having a structure capable of receiving a polar organic liquid, with an acid and with an admixture of a polar organic liquid having a polarity index greater than about 1.5 but less than that of water and a non-polar organic liquid. 24. The method in accordance with claim 23 wherein the polar organic liquid is a member of the group consisting of an aliphatic C x to C 6 monohydric alcohol and an aliphatic C 2 to C 6 ether, and wherein non-polar organic liquid is an aliphatic hydrocarbon. 25. The method in accordance with claim 23 wherein the polar organic liquid is ethanol and the n poplar organic liquid is n-heptane. 26. The method in accordance with claim 23 wherein the polar organic liquid is isopropyl alcohol and the non-polar organic liquid is n-hexane. 27. The method in accordance with claim 23 wherein the polar organic liquid and the non-polar organic liquid form an azeotrope. 28. The method in accordance with claim 27 wherein the azeotrope is ethanol/n-hexane azeotrope. 29. The method in accordance with claim 27 wherein the azeotrope is ethanol/n-heptane azeotrope.

Inventors: BROOKS DAVID D, HANSEN DARLENE M, SHAKED DOV, BROOKS, DAVID, D., HANSEN, DARLENE, M., SHAKED, DOV
Applicants: OIL DRI CORP OF AMERICA, OIL-DRI CORPORATION OF AMERICA
Application year: 1995
Main classification: C04B14
IPC codes: B01J20