Sulfone Peroxycarboxylic Acids

In the following examples, which illustrate the invention, and throughout the specification, parts and percent are by weight unless otherwise indicated.

To a 1000 mL 4 neck glass reaction flask equipped with a mechanical stirrer, dropping funnel, thermometer, water cooled condenser, and ice bath were charged 100.18 g of cyclohexylmercaptan and 1 mL of 40% aqueous benzyltrimethylammonium hydroxide solution (as catalyst). To the dropping funnel was charged 84.15 mL (10% excess) of methyl acrylate. With agitation and ice cooling the methyl acrylate was added over a period of 14 minutes at 28.degree.-38.degree. C. Following the addition, the ice bath was replaced by a heating mantle, and agitation was continued at 30.+-.1.degree. C. for 69 minutes. 171.1 mL of 20% aqueous NaOH was charged to the dropping funnel, and 278 mL of absolute ethanol was charged to the reactor. The NaOH (10% excess over methyl acrylate) was added over a period of 9 minutes, the temperature rising to 46.5.degree. C. The mixture was heated to reflux (80.degree. C.) and refluxed for 46 minutes. The mixture was cooled to 25.degree. C. and transferred (with H.sub.2 O rinse) to a rotary evaporator. Using aspirator vacuum and a bath temperature of 50.degree.-55.degree. C., 280 mL of volatile material (mostly ethanol) was stripped off and discarded. The residue was a homogeneous, water white solution weighing 360.3 g. The residue was cooled in an ice bath, transferred to a 1000 mL separatory funnel, and reacted therein with 95.8 mL of cold 37% aqueous HCl (10% excess over NaOH). Enough dry NaCl was added in several portions to nearly saturate the aqueous phase. After cooling, shaking, and settling for 30 minutes, the mixture consisted of an upper oil phase containing the bulk of the product and a lower aqueous phase which was drained off and discarded. The oil phase was washed once with an equal volume of nearly saturated aqueous NaCl, and after settling overnight, the wash layer was drained off and discarded. The oil phase was transferred to a 2000 mL 4 neck glass reaction flask, fitted with a dropping funnel, mechanical agitator, alcohol thermometer, reflux condenser, and an ice bath. 860 mL of glacial acetic acid was also charged, part of it being used to rinse residues from the separatory funnel into the reactor. To the dropping funnel was charged 133.3 mL of 30% H.sub.2 O.sub.2 (50% excess over theoretical for conversion to the sulfoxide). The H.sub.2 O.sub.2 was added with agitation over a period of 22 minutes with cooling as needed to maintain .ltoreq.32.degree. C. Following the addition, agitation was continued without cooling for 68 minutes, the temperature declining to 25.5.degree. C. Leaving a small heel in the reactor, most of the reaction mixture was transferred to a 4000 mL beaker and mixed with another 133.3 mL of 30% H.sub.2 O.sub.2 (no temperature rise observed). The heel was heated to reflux, and the mixture from the beaker was added to the reactor via the dropping funnel over a period of 37 minutes. Refluxing was continued for another 60 minutes, and the mixture was then cooled to room temperature.

Another 102 mL of 30% H.sub.2 O.sub.2 was added and mixed in, and the mixture was allowed to stand for 41/2 days at ambient temperature. Excess H.sub.2 O.sub.2 was destroyed by mixing with 900 mL water and 219.18 g Na.sub.2 SO.sub.3 in a 4000 mL beaker at .ltoreq.50.degree. C. The liquid phase was separated from undissolved salts by a combination of decantation and filtration and transferred to a rotary evaporator (in several batches) where volatiles were stripped off at a bath temperature of 51.degree.-52.degree. C. (aspirator vacuum) and discarded. The residue, a thin sludge, became a solid crystalline mass upon cooling and standing. The total product was collected in a 4000 mL beaker and diluted with water to 1000 mL. This mixture was heated to 80.degree. C., at which temperature it was a homogeneous solution. It was then cooled to 18.degree. C., at which temperature it crystallized rapidly to form a thick white slurry. The solids were collected by filtration at 15.degree.-20.degree. C., washed on the filter with water, and dried at ambient temperature to constant weight. The product weighed 129.12 g, equivalent to a yield of 68% of theory based upon the amount of cyclohexylmercaptan used. Analysis by NMR in DMSO-D6 confirmed that the product was 3-(cyclohexylsulfonyl)propionic acid, free of detectable amounts of impurities or retained water.

To a 150 mL beaker equipped with a support clamp, ice bath, alcohol thermometer, mechanical stirrer, and dropping funnel were charged 22.03 g (0.1 mole) of powdered 3-(cyclohexylsulfonyl)propionic acid and 29.8 mL of 82 wt. % aqueous H.sub.2 SO.sub.4. After a few minutes mixing at ambient temperature, a uniform slurry was obtained. To the dropping funnel was charged a solution prepared by adding 33.3 mL of 95.5% H.sub.2 SO.sub.4 to 17.0 mL of 50% H.sub.2 O.sub.2 (0.3 mole, 3 fold excess) with stirring and cooling to maintain .ltoreq.30.degree. C., with final cooling to 25.degree. C. With agitation, the mixture in the dropping funnel was added to the beaker over a 10 minute period, the temperature rising to 27.degree. C. The ice bath was not applied because the heat evolution was so small. The mixture was agitated for another 130 minutes, the temperature gradually declining to 26.5.degree. C. Most of the solids dissolved. The mixture was then contacted with ten 25-30 mL portions of methylene chloride at ambient temperature in an effort to recover the product by direct extraction into the methylene chloride. The combined extracts were washed with pH 5 phosphate buffer solution, then washed with water, partially evaporated, mixed with a weighed amount of boric acid, and dried. The weight and active oxygen analysis of this product showed that only 3.57 g of the organic product had been recovered by extraction (.about.15% of theory) and that its activity was 91.1% of that for the pure peracid. The crude reaction product remaining after methylene chloride extraction was mixed with 100 mL of cold pH 5 buffer with agitation and ice cooling, resulting in immediate formation of a large amount of white solids. The slurry was filtered at 15.degree.-20.degree. C. and the solids were washed on the filter with two 100 mL portions of cold buffer followed by 100 mL cold water. The resulting product was mixed with boric acid and dried and then blended uniformly with most of the product recovered by extraction. The resulting final product weighed about 30 g and had an active oxygen content (iodometric titration) of 3.27% (boric acid content roughly 47%). The calculated active yield was 61% of theory, where active yield=percent active oxygen/theoretical percent active oxygen X product weight/theoretical product weight X 100.

A mixture of 5 g of 4-(methylthio)benzoic acid (97%) and 30 mL of glacial acetic acid was formed. The mixture was cooled in a water bath containing a small amount of ice. To the mixture was added 8.5 g of 30% hydrogen peroxide gradually over one hour. No temperature rise was observed during the addition of the hydrogen peroxide. The reaction mixture was then heated for one and a half hours with the temperature ranging between 70.degree. C. and 100.degree. C. Heating was stopped and the reaction mixture was allowed to cool to room temperature. A solid was present in the reaction mixture. A solution of 3 g of sodium sulfite in 57 g of water was added to the reaction mixture. The solid was filtered from solution and was washed three times with cold deionized water. The solid was transferred to a watchglass and dried overnight. The dried product weighed 5.25 g which is a yield of 88.1% of the theoretical based upon the amount of the starting benzoic acid.

An NMR spectrum of the product in deuterated dimethylsulfoxide was in agreement with a literature spectrum of the compound in the same solvent ("Aldrich Library of NMR Spectra").

This batch of product was combined with the product from a larger scale batch (4x). The combined products were recrystallized from ethanol. The recrystallized material was used in the synthesis of 4-(methylsulfonyl)peroxybenzoic acid.

A stirred mixture of 5 g of 4-(methylsulfonyl)-benzoic acid and 50 mL of methanesulfonic acid froze when it was cooled in an ice bath. The ice bath was removed and when the mixture was partially melted, stirring was resumed and the addition of 2.83 g of 90% hydrogen peroxide was started. The 90% hydrogen peroxide was added gradually over ten minutes. When the addition of the hydrogen peroxide was completed, the reaction mixture was still partially frozen. A water bath of cold tap water was used to warm the reaction mixture. The temperature of the reaction mixture rose briefly to 28.degree. C. One hour after the addition of the hydrogen peroxide was started, the reaction mixture was heated for 70 minutes within a temperature range of 40.degree. C.-45.degree. C. The stirred reaction mixture was then cooled in an ice bath. A solid precipitated from solution. When the temperature of the reaction mixture was between 10.degree. C.-15.degree. C., the solid product was filtered from solution. A second fraction of solid product was collected when the filtrate was poured onto ice prepared from deionized water and the solid which formed was filtered away from solution. Fraction one was washed four times with 60 mL each time of cold deionized water. Fraction two was washed four times with 150 mL each time of cold deionized water. Both fractions of the solid product were very easy to wash and to isolate by filtration. The two fractions were each transferred to a watchglass and dried overnight. The dried solids were fine, dry powders.

The two fractions were combined and an equal weight of boric acid powder was added. The mixture was put through a #30 polyethylene sieve. Particle size would be <600 microns. The mixture was then bottled and the bottle was shaken to blend well the boric acid with the product.

Percent by weight of active oxygen in the boric acid-stabilized product was 3.31%.

A mixture of 200 g of 11-bromoundecanoic acid, 60 g of thiourea and 600 mL of absolute ethanol was stirred and heated at reflux for two hours. After heating was stopped a solution of 80 g of sodium hydroxide in 250 mL of water was then added dropwise. The mixture was held overnight and then heated at reflux for three hours. After cooling to room temperature a solid precipitated from solution. The reaction mixture was poured into a mixture of ice and 200 g of concentrated hydrochloric acid. The solids were filtered from solution then slurried with ice water, isolated by filtration and washed twice. The off-white solid was stored in a crystallizing dish for one week, then dried under vacuum (.about.1 mm of Hg) at about 45.degree. C. The product was distilled under vacuum (.about.1 mm of Hg at .about.160.degree. C.). NMR analysis indicated the desired product was obtained. The distilled product weighed 74.7 g representing 45.46% yield based upon the weight of starting 11-bromoundecanoic acid.

Into a 3-neck round-bottom flask fitted with a condenser and an addition funnel were added 20 g of 11-mercaptoundecanoic acid, 13 g of methyl iodide and 200 mL of ethanol. A slow flow of nitrogen through the reactor was started to exclude oxygen because mercaptans can be converted into disulfides in the presence of air and strong alkali. A solution of 7.33 g of sodium hydroxide in 14.66 g of water was added dropwise to the reaction mixture via the addition funnel. Any unreacted methyl iodide, the ethanol and the water were removed using a rotovap. The residue was acidified using a mixture of concentrated hydrochloric acid and ice. After isolation the product was distilled. After a small amount of a low boiling fraction was collected, the crude product was collected at .about.1 mm of Hg at 180.degree. C. weighing 22.75 g. The crude product was distilled to yield 12.5 g of desired product representing 58.7% of theoretical based upon the weight of starting 11-mercaptoundecanoic acid.

Into a three-neck round-bottom flask fitted with an overhead mechanical stirrer, thermometer and addition funnel were added 12.3 g of 11-(methylthio)-undecanoic acid and 53 mL of acetic acid. The mixture was warmed slightly to help all of the solid to dissolve in the acetic acid. At a temperature of approximately 30.degree. C., the dropwise addition of 24 g of 30% hydrogen peroxide was started. After the addition was completed, the reaction mixture was stirred without heating for an hour. The mixture was then heated at slow reflux for an hour. The reaction mixture was cooled first to room temperature and then in an ice bath. Aqueous sodium sulfite (5%) was added to decompose all active oxygen present. The solid was filtered and washed several times with cold deionized water. The solid was then dried overnight on a watchglass. The product weighed about 7.7 g (55% of theoretical) based upon the weight of starting acid.

A stirred mixture of 3 g of 11-(methylsulfonyl)undecanoic acid and 30 mL of methanesulfonic acid was heated to approximately 40.degree. C. The solid dissolved only partially in the methanesulfonic acid at this temperature. Then 1.29 g of 90% hydrogen peroxide was added dropwise. The temperature of the reaction mixture was reduced to room temperature after twenty minutes of reaction time. For the remainder of the two hour reaction time, the reaction mixture was not heated and became homogeneous. The reaction mixture was then cooled in an ice bath forming a solid which was then filtered from solution. The filtrate was poured onto ice prepared from distilled water. A solid formed which was filtered from solution. The two solids collected were combined and washed several times with cold deionized water until the filtrate was no longer strongly acidic. The solid was dried overnight on a watchglass, weighed 2.91 g and had 4.8% by weight active oxygen (84.1% of theoretical).

To a 250 mL round-bottomed flask fitted with an overhead mechanical stirrer, a thermometer and an addition funnel were charged 87 g of 1-decanethiol and 20 drops of a 21% by weight solution of sodium ethoxide in ethanol. The mixture was cooled to 10.degree. C. using an ice bath. Then the dropwise addition of 53 g of acrylonitrile was started. After addition of a portion of the acrylonitrile, 10 drops of 21% by weight solution of sodium ethoxide in ethanol were added. The temperature of the reaction mixture during the addition of the remaining acrylonitrile ranged between 30.degree. C. and 35.degree. C. The reaction mixture was then kept at room temperature overnight (.about.19 hours). The unreacted acrylonitrile was then removed by distillation at atmospheric pressure. The remaining material was then distilled at .about.1 mm pressure. A first fraction was collected from 150.degree. C. to 160.degree. C. Fraction one had a strong odor of thiol. A second and final fraction was collected at 160.degree. C. The second fraction had a faint odor of thiol. An NMR spectrum indicated the second fraction to be the desired product 83.5% of theoretical (94.9 g) based upon the weight of 1-decanethiol employed.

The product of Example 9 was converted to the corresponding carboxylic acid by alkaline hydrolysis followed by acidification and then to the corresponding sulfone carboxylic acid by oxidation in accordance with a procedure found in U.S. Pat. No. 3,857,875 to Brady et al. A stirred mixture of 5 g of 3-(n-decylsulfonyl)propionic acid and 50 mL of methanesulfonic acid was heated to 40.degree..+-.3.degree. C. The 3-(n-decylsulfonyl)propionic acid dissolved only partially in the methanesulfonic acid at this temperature. Then 2.04 g of 90% hydrogen peroxide was added dropwise via pipette over ten minutes. Before the addition of the hydrogen peroxide was completed, the reaction mixture became thick from precipitation of a solid. After the addition of the 90% hydrogen peroxide was completed, the heating of the reaction mixture was continued at 40.degree..+-.3.degree. C. until the reaction time totalled ninety minutes beginning at the start of the addition of the hydrogen peroxide. The reaction mixture was then cooled in an ice bath at 10.degree. C. The solid was then filtered from solution using a coarse sintered-glass funnel, then transferred to a beaker containing 200 mL of ice water prepared from deionized water. The product was washed twice with ice water, filtered and dried to provide 4.63 g of the desired product (87.6% of theoretical based upon the weight of starting 3-(n-decylsulfonyl)propionic acid). The product was found to have 5.32% active oxygen. The product was stabilized with an equal weight of boric acid and put through a #30 polyethylene sieve which provided a particle size of less than 600 microns. The stabilized product contained 2.58% by weight active oxygen.

An apparatus was provided including a two liter, 4-neck, round bottom flask equipped with an alcohol thermometer, an overhead mechanical stirrer, a water-cooled condenser and a nitrogen purge. Into this reactor gradually were added 23 g of sodium into 1,200 ml of absolute ethanol previously added. After all of the sodium had reacted the solution was stirred overnight under a slow nitrogen flow. 1-octanethiol, 146.28 g, was added to the mixture and an addition funnel and heating mantel were added to the reactor. In 200 ml of ethanol, 129.13 g of butyrolactone was added dropwise to the ethanol solution at reflux temperature. The resulting mixture was heated at reflux overnight. The ethanol was then removed from the reaction mixture and the residue was dissolved in water. The aqueous solution was washed with methylene chloride. The aqueous solution was then added to an ice/sulfuric acid mixture and the product extracted with methylene chloride. The methylene chloride solution was washed with water, dried with sodium sulfate, filtered and concentrated under vacuum with heating. The liquid product solidified upon cooling to room temperature. There was provided 219 g of 4-(n-octylthio)butyric acid. The solid exhibited a melting point of 33.degree.-34.5.degree. C.

The acid produced as described above, 232.37 g, was added to a reactor which was a 2 liter, 4-neck round bottom flask equipped with an alcohol thermometer and overhead mechanical stirrer with a glass rod and teflon blade, a water cooled condenser, an addition funnel and a nitrogen purge. The reactor was provided with an ice bath. The reactor was charged with 900 ml of glacial acetic acid and the sulfide. The stirred mixture was cooled to 10.degree. C. and dropwise addition of 30% hydrogen peroxide was started and continued until 183 g of the peroxide were added. An exotherm reaction was noted and the temperature of the mixture was kept at or below 30.degree. C. during the hydrogen peroxide addition. After stirring the mixture for 1 hour a heating mantle was added to provide a reaction mass temperature of between 90.degree.-95.degree. C. An exothermic reaction occurred and the heating mantel was removed. At the end of the exothermic reaction the heating continued to maintain a reaction temperature of about 90.degree. C. for one hour. The mixture was cooled to provide 165.8 g of the solid 4-(n-octylsulfonyl)butyric acid. The acid demonstrated the melting point of 124.degree.-125.degree. C. This acid (125 g) was then reacted with 68.93 g of 70% hydrogen peroxide in 1.25 liters of methanesulfonic acid to provide 4-(n-octylsulfonyl)peroxybutyric acid. The resulting product indicated 5.43% active oxygen and had a melting point of 113.degree.-115.degree. C.

To a 2,000 ml 4-neck glass reaction flask

equipped with a stirrer, dropping funnel, thermometer, and condenser protected by a N.sub.2 purge was charged 212.08 g of n-decanethiol (97%). With agitation at ambient temperature, 2.0 ml of 40% aqueous benzyltrimethylammonium hydroxide was added as a catalyst. Via the dropping funnel, 152.2 ml of dimethylmaleate (96%) was then added over a period of 50 minutes, with ice cooling to maintain below about 40.degree. C. The resulting homogeneous solution was then stirred at 37.degree.-41.degree. C. for another 95 minutes. Following this hold period, 500 ml of absolute ethanol was mixed in rapidly, resulting in a slightly turbid, pale yellow solution at 26.5.degree. C. Next, 268.8 ml of 30% aqueous NaOH was added over a period of 74 minutes with agitation and mild heating, resulting in a temperature of 62.degree. C. at the end of the addition. The resulting thick white slurry was diluted with 235 ml of water and heated to reflux (81.0.degree. C.), resulting in dissolution of the solids. Refluxing was then continued for 40 minutes. The resulting solution was further diluted with 500 ml of water and cooled to 40.degree. C. Using a rotary evaporator, a total of 809.5 ml of ethanol and H.sub.2 O were stripped off. The bottom fraction was transferred to a 4,000 ml beaker and diluted with more water to obtain about 2,000 ml of a turbid solution consisting mainly of water and the sodium salt of decylthiosuccinic acid. Some residual decanethiol was also present, and most of this was removed by extraction into about 700 ml of petroleum ether. Rag layers were treated with additional water, resulting in further separation of petroleum ether, and then combined with the aqueous phase. A small amount of NaCl added to the washed aqueous phase resulted in some precipitation of solids. The volume of the resulting slurry was about 3,200 ml. To this slurry, 235 ml of 37% HCl was added dropwise with agitation and ice cooling to maintain a temperature of from 12.degree.-17.degree. C. Agitation was then continued for another hour at 15.degree. C. The resulting solids were collected by filtration, washed with a total of 3,500 ml of water (pH of final filtrate was about 3), and dried at ambient temperature for about 221/4 hours. The resulting white, granular, free flowing solids with a mild sulfide odor weighed 608.9 g. Analysis by NMR in DMSO-D6 and by the Karl Fisher method for water content showed that the product was C.sub.10 H.sub.21 SCH(COOH)CH.sub.2 COOH.12H.sub.2 O. Thus, the amount recovered was 98.8% of the theoretical amount (without correction for assay of starting materials). The only detectable impurity was a trace of fumaric acid.

In a 400 ml beaker equipped with a heating mantle, alcohol thermometer, 50 ml dropping funnel, and a stirrer, 100 ml of glacial acetic acid was heated to about 50.degree. C. To this was added 101.32 g of the dry solid C.sub.10 H.sub.21 SCH(COOH)CH.sub.2 COOH.12H.sub.2 O described above, with stirring and heating to obtain a thick white slurry. Via the dropping funnel, 22.64 ml of 70% H.sub.2 O.sub.2 was then added over a period of 114 minutes at 45.degree.-53.degree. C., resulting in an exothermic reaction. Agitation was then continued for 31/2 hours at 47.degree.-53.degree. C. The resulting homogeneous solution was diluted with 50 ml of water and then cooled to ambient temperature, becoming a thick white slurry which was then held overnight. The slurry was cooled to 5.degree.-10.degree. C., and the solids were collected by filtration. The solids were dissolved in 515 ml of ethyl acetate. This solution was filtered to remove a small amount of insoluble material, washed with three 200 ml portions of water and transferred to a 4,000 ml beaker. Enough ethylacetate was then boiled off to reduce the solution volume to about 300 ml. Heating was discontinued, and with agitation, 1,500 ml of petroleum ether was added via a dropping funnel, resulting in the precipitation of a white solid product. The slurry was cooled to 5.degree.-10.degree. C., and the solids were recovered by filtration. The solids were washed by reslurrying in petroleum ether, again recovered by filtration, and dried overnight at ambient temperature. The resulting product weighed 34.63 g, and NMR analysis in DMSO-D6 showed that it was n-decylsulfonylsuccinic acid, C.sub.10 H.sub.21 SO.sub.2 CH(COOH)CH.sub.2 COOH. Water was not present at detectable levels, and the only detectable impurity was about 0.2% of fumaric acid. The yield was 53.7% of the theoretical amount, based upon the amount of the sulfide used.

To a 400 ml beaker equipped with a heating mantle, alcohol thermometer, 50 ml dropping funnel, stirrer, and loose cover were charged 32.24 g of C.sub.10 H.sub.21 SO.sub.2 CH(COOH)CH.sub.2 COOH and 150 ml of 99.5% methanesulfonic acid (MSA). The resulting slurry was heated to 51.degree. C., and via the dropping funnel, about 3.0 ml of 70% H.sub.2 O.sub.2 was added over a period of about 15 minutes, the temperature rising to 53.degree. C. H.sub.2 O.sub.2 addition was stopped, and agitation was continued at 53.degree. C. for two minutes, at the end of which time most of the solids

had dissolved. The mixture was cooled to 29.5.degree. C, and addition of H.sub.2 O.sub.2 was resumed. Total H.sub.2 O.sub.2 addition was 22.64 ml. The last 19.64 ml of H.sub.2 O.sub.2 were added over a period of 30 minutes, with cooling to maintain 28.degree.-30.degree. C., and about halfway through this addition a large additional amount of white solids precipitated rapidly. Following the addition, agitation was continued for two hours at 26.degree.-29.degree. C. The crude slurry was diluted several times with CH.sub.2 Cl.sub.2 (total volume 428 ml) followed by filtration in an attempt to remove MSA. These filtrations were difficult and incomplete. The resulting wet filter cake was washed several times by mixing with petroleum ether and decanting off the upper layer. The cake was then totally dissolved in ethyl acetate, and this solution was washed three times with 100 ml portions of water. A small amount of NaH.sub.2 PO.sub.4.H.sub.2 O was added to promote phase separation after the third wash. Most of the washed ethyl acetate solution was transferred to an evaporating dish, and most of the solvent was evaporated. The damp residual solids were mixed with 6.28 g of powdered boric acid, and the mixture was dried overnight at ambient temperature. The resulting product weighed 20.22 g, and its active oxygen content was 3.83%. It is estimated that the product contained about 31.06% boric acid. Based upon this, the measured activity was about 61.6% of the theoretical value for such a mixture in which the organic fraction is pure dry C.sub.10 H.sub.21 SO.sub.2 CH(CO.sub.3 H)CH.sub.2 CO.sub.3 H.

In all of the tests below a detergent is employed as a control at a use level of 1.5 g/L of wash solution. Various bleach compounds of this invention were added to portions of the detergent composition in the amounts shown below in the tables. Each test series contained a control. The detergent formulation is as follows:

All of the examples below were conducted at the same wash conditions of 100.degree. F. and with water having a hardness level of 150 ppm (3:2 mole ratio of calcium to magnesium calculated as calcium carbonate). In each test a set of three swatches were evenly stained. After staining, the light reflectance value (Rd.sub.i) was measured using the Gardner XL-23 Tristimulator Colorimeter manufactured by Gardner Laboratory, Inc., Bethesda, Md.

A Terg-o-tometer was employed to test the bleaching performance of the bleach compounds. In each test three stained swatches together with three unstained swatches were placed in a cylindrical container with 1 liter of water and 1.5 g of detergent together with a weighed amount of a bleach compound of this invention. Two minutes were allowed for the detergent to dissolve. The washing operation covered a period of 10 minutes after which the laundered swatches were rinsed with clear water and dried. Light reflectance measurements of each cleaned dried swatch were made and averaged (Rd.sub.f). The difference (.DELTA.Rd) of these readings for each type of stain is reported in the tables below. (.DELTA.Rd=Rd.sub.f -Rd.sub.i)

The bleach compounds employed in the following examples are represented by the following structure wherein A and B are defined in the tables below. ##STR15##

The tests in Tables I and II below are separate and each includes a control result. In some instances compounds of this invention employed in the separate tests were prepared at different times and in small amounts. The results of each test are comparable only within the context of the individual tests with control data unless otherwise noted. In Tables I and II below the fabric type and kind of stain are listed at the top of each column of data. The notation of poly/cotton means a fabric blend having a ratio of 50:50 of polyester and cotton.

In addition to .DELTA.Rd data there is reported in the Tables below the percent soil removal (%SR) which may be related to visual effect. Percent soil removal reported in the Tables below was calculated according to the formula: ##EQU1## wherein Rd.sub.i is the reflectance data obtained by measuring the reflectance of the test swatches after staining but before bleaching in accordance with the procedure described above.

The stain removal test of Example 13 was repeated with a series of alkylsulfonyl peroxypropionic acids prepared by methods similar to Example 10. In Table III below there is presented the results of the stain removal tests and the percent improvement in stain removal over the results obtained with the detergent control formulation without bleach. The detergent formulation was the same as described in Example 13. The peroxyacids were employed as 50:50 mixtures with boric acid and exhibited active oxygen in the range of from about two (2) to about four (4) percent, by weight. The peroxyacid concentration was sufficient to provide 8 ppm active oxygen concentration in the wash bath. The stains tested were tea on cotton, coffee on polyester-cotton blend described above and clay on cotton. The results in Table III below are presented as an average of all results.

Improved stability of the compounds of this invention are shown by several test procedures described below. In one such test a value "t.sub.50 " is determined which is a measure of the amount of time required for a bleach compound to lose 50% of its originally determined amount of active oxygen. This value is measured for peroxyacids and formulations thereof by incubating the samples in open glass vials at 39.degree. C. and 85% relative humidity. At periodic intervals, aliquot samples are taken and percent active oxygen (% AO) is measured by iodometric titration.

A plot of A/A.sub.0 versus time where A=% AO@t=incubation time and A.sub.0 =% AO@t=0 generates a curve which shows the decomposition of the peracid. Since most organic peracids decompose via an accelerating autocatalytic route, storage stability is reported as "t.sub.50 ".

Data for several of the sulfone peroxycarboxylic acids and, for comparison, several prior art peracids are presented below in Table IV.

Other determinations were obtained from the above-described test by calculating data from the plot A/Ao to determine the amount of active oxygen in the sample after a period of 30 days. The results are reported in Table IV as the percentage of the original amount of active oxygen in the sample.

In another procedure the temperature of onset of self-heating for bleach compounds and formulations thereof was determined by the following procedure employing accelerating rate calorimetery (ARC). In this procedure samples to be tested are monitored for temperature changes as they are heated in stepped increments of five degrees centigrade. After each step ten minutes is allowed for thermal equilibrium to occur followed by a hold time of twenty minutes at adiabatic conditions. This method continues until the onset of self-heating is observed. The results of this test appear in Table V under the column marked "A.R.C.". Several known prior art bleaches were included for comparison.

In addition to the compounds of this invention described by the above examples, any number of other compounds are contemplated to be within the spirit and scope of this invention. Some examples of such compounds are represented by the formulae below: ##STR21##

The sulfone peroxycarboxylic acids can be employed alone or be combined with other materials in any number of ways to produce formulated products. Examples of such formulated products include but are not limited to complete laundry detergents, dry bleach formulations, machine dishwashing formulations, bleach releasing articles such as pouches, fabric sheets, and the like, bleaching formulations for use in dry cleaning operations, products for use in textile or paper manufacture, hard surface cleaners, and the like. Among other known ingredients typically employed in such formulations are stabilizers, chelating agents, solubilizers, surfactants, diluents, detergent builders, fragrances, pH adjustment agents, abrasives, optical brighteners, coloring agents, exotherm control agents, solvents, encapsulation agents, enzymes, etc. All such formulations which comprise a bleach effective amount of a sulfone peroxycarboxylic acid are within the scope of this invention. It is obvious that materials selected to provide the above formulations must be compatible with peroxycarboxylic acids of this invention or means must be taken to segregate the material from the bleach.

Typical pH adjustment agents are used to alter or maintain aqueous solutions of the instant compositions during use within the 5 to10 pH range in which peroxyacid bleaching agents are generally most effective. Depending upon the nature of other optional composition ingredients, pH adjustment agents can be either of the acid or base type. Examples of acidic pH adjustment agents designed to compensate for the presence of other highly alkaline materials include normally solid organic and inorganic acids, acid mixtures and acid salts. Examples of such acidic pH adjustment agents include citric acid, glycolic acid, sulfamic acid, sodium bisulfate, potassium bisulfate, ammonium bisulfate and mixtures of citric acid and lauric acid. Citric acid is preferred by virtue of its low toxicity and hardness sequestering capability.

Optional alkaline pH adjustment agents include the conventional alkaline buffering agents. Examples of such buffering agents include such salts as carbonates, bicarbonates, phosphates, silicates and mixtures thereof.

Since the peroxyacid compounds used in the compositions of the present invention are subject to the loss of available oxygen when contacted by heavy metals, it is desirable to include a chelating agent in the compositions. Such agents are preferably present in an amount ranging from about 0.005% to about 1.0% based on the weight of the composition. The chelating agent can be any of the well known agents, but certain are preferred. U.S. Pat. No. 3,442,937, May 6, 1969, to Sennewald et al, discloses a chelating system comprising quinoline or a salt thereof, an alkali metal polyphosphate, and, optionally, a synergistic amount of urea. U.S. Pat. No. 2,838,459, July 10, 1958, to Sprout, Jr., discloses a variety of polyphosphates as stabilizing agents for peroxide baths. These materials are useful herein. U.S. Pat. No. 3,192,255, June 29, 1965, to Cann, discloses the use of quinaldic acid to stabilize percarboxylic acids. This material, as well as picolinic acid and dipicolinic acid, would also be useful in the compositions of the present invention. A preferred chelating system for the present invention is the alkali metal polyphosphate system.

In addition to the above-mentioned chelating systems to tie up heavy metals in the peroxyacid compositions, coating materials (encapsulating agents) may also be used as stabilizers to extend the shelf life of dry granular compositions. Such coating materials may be in general, acids, esters, and hydrocarbons and include such things as wide varieties of fatty acids, derivatives of fatty alcohols such as esters and hydrocarbon oils and waxes. These materials aid in preventing moisture from reaching the peroxyacid compound. Secondly, the coating may be used to segregate the peroxycarboxylic compound from other agents which may be present in the composition and adversely affect the peroxycarboxylic's stability. The amount of the coating material used is generally from about 2.5% to about 15% based on the weight of the peroxycarboxylic acid compound.

It is known to combine peroxycarboxylic acids with exotherm control agents to prevent runaway reaction in the event of overheating, etc. The use of boric acid as an exotherm control agent has been described in U.S. Pat. No. 4,100,095, issued July 11, 1978 to Hutchins et al. Other possible exotherm control agents include hydrates of salts such as magnesium sulfate, calcium sodium sulfate, magnesium nitrate, potassium aluminum sulfate, and aluminum sulfate, and the like as disclosed in U.S. Pat. No. 3,770,816, issued Nov. 6, 1973 to Nielson. Such materials may be employed in conjunction with sulfone peroxycarboxylic acids.

Agents which improve the solubility of the sulfone peroxycarboxylic acid product such as sodium sulfate, starch, cellulose derivatives, surfactants, etc., are also advantageously used herein. These agents can be called solubilizers and are generally used in an amount of from about 10% to about 200% based on the weight of the peroxyacid.

Optional materials for the instant bleaching compositions can include such standard detergent adjuvants as surfactants and builders. Optional surfactants are selected from the group consisting of organic anionic, nonionic, ampholytic, and zwitterionic surfactants and mixtures thereof. Optional builder materials include any of the conventional organic and inorganic builder salts including carbonates, silicates, acetates, polycarboxylates and phosphates. If the instant stabilized bleaching compositions are employed as part of a conventional fabric laundering detergent composition, the instant bleaching system generally comprises from about 1% to about 40% by weight of such conventional detergent compositions. Conversely, the instant bleaching compositions can optionally contain from about 60% to about 99% by weight of conventional surfactant and builder materials. Further examples of suitable surfactants and builders are given below.

Water-soluble salts of the higher fatty acids, i.e., "soaps", are useful as the anionic surfactant herein. This class of surfactants includes ordinary alkali metal soaps such as the sodium, potassium, ammonium and alkanolammonium salts of higher fatty acids containing from about 8 to about 24 carbon atoms and preferably from about 10 to about 20 carbon atoms. Soaps can be made by direct saponification of fats and oils or by the neutralization of free fatty acids. Particularly useful are the sodium and potassium salts of the mixtures of fatty acids derived from coconut oil and tallow, i.e., sodium or potassium tallow and coconut soaps.

Another class of anionic surfactants includes water-soluble salts, particularly the alkali metal, ammonium and alkanolammonium salts, of organic sulfuric reaction products having in their molecular structure an alkyl group containing from about 8 to about 22 carbon atoms and a sulfonic acid or sulfuric acid ester group. (Included in the term "alkyl" is the alkyl portion of acyl groups.) Examples of this group of synthetic surfactants which can be used in the present detergent compositions are the sodium and potassium alkyl sulfates, especially those obtained by sulfating the higher alcohols (C.sub.8 -C.sub.18 carbon atoms) produced by reducing the glycerides of tallow or coconut oil; and sodium and potassium alkyl benzene sulfonates, in which the alkyl group contains from about 9 to about 15 carbon atoms in straight chain or branched chain configuration, e.g., those of the type described in U.S. Pat. Nos. 2,220,099, and 2,477,383, incorporated herein by reference.

Other anionic surfactant compounds useful herein include the sodium alkyl glyceryl ether sulfonates, especially those ethers or higher alcohols derived from tallow and coconut oil; sodium coconut oil fatty acid monoglyceride sulfonates and sulfates; and sodium or potassium salts of alkyl phenol ethylene oxide ether sulfate containing about 1 to about 10 units of ethylene oxide per molecule and wherein the alkyl groups contain about 8 to about 12 carbon atoms.

Other useful anionic surfactants herein include the water-soluble salts of esters of .alpha.-sulfonated fatty acids containing from about 6 to 20 carbon atoms in the ester group; water-soluble salts of 2-acyloxy-alkane-1-sulfonic acids containing from about 2 to 9 carbon atoms in the acyl group and from about 9 to about 23 carbon atoms in the alkane moiety; alkyl ether sulfates containing from about 10 to 20 carbon atoms in the alkyl group and from about 1 to 30 moles of ethylene oxide; water-soluble salts of olefin sulfonates containing from about 12 to 24 carbon atoms; and .beta.-alkyloxy alkane sulfonates containing from about 1 to 3 carbon atoms in the alkyl group and from about 8 to 20 carbon atoms in the alkane moiety.

Preferred water-soluble anionic organic surfactants herein include linear alkyl benzene sulfonates containing from about 11 to 14 carbon atoms in the alkyl group; the tallow range alkyl sulfates; the coconut range alkyl glyceryl sulfonates; and alkyl ether sulfates wherein the alkyl moiety contains from about 14 to 18 carbon atoms and wherein the average degree of ethoxylation varies between 1 and 6.

Specific preferred anionic surfactants for use herein include: sodium linear C.sub.10 -C.sub.12 alkyl benzene sulfonate; triethanolamine C.sub.10 -C.sub.12 alkyl benzene sulfonate; sodium tallow alkyl sulfate; sodium coconut alkyl glyceryl ether sulfonate; and the sodium salt of a sulfated condensation product of tallow alcohol with from about 3 to about 10 moles of ethylene oxide.

It is to be recognized that any of the foregoing anionic surfactants can be used separately herein or as mixtures.

Nonionic surfactants include the water-soluble ethoxylates of C.sub.10 -C.sub.20 aliphatic alcohols and C.sub.6 -C.sub.12 alkyl phenols. Many nonionic surfactants are especially suitable for use as suds controlling agents in combination with anionic surfactants of the type disclosed herein.

Semi-polar surfactants useful herein include water-soluble amine oxides containing one alkyl moiety of from about 10 to 28 carbon atoms and 2 moieties selected from the group consisting of alkyl groups and hydroxyalkyl groups containing from 1 to about 3 carbon atoms; water-soluble phosphine oxides containing one alkyl moiety of about 10 to 28 carbon atoms and 2 moieties selected from the group consisting of alkyl groups and hydroxyalkyl groups containing from about 1 to 3 carbon atoms; and water-soluble sulfoxides containing one alkyl moiety of from about 10 to 28 carbon atoms and a moiety selected from the group consisting of alkyl and hydroxyalkyl moieties of from 1 to 3 carbon atoms.

Ampholytic surfactants include derivatives of aliphatic or aliphatic derivatives of heterocyclic secondary and tertiary amines in which the aliphatic moiety can be straight chain or branched and wherein one of the aliphatic substituents contains from about 8 to 18 carbon atoms and at least one aliphatic substituent contains an anionic water-solubilizing group.

Zwitterionic surfactants include derivatives of aliphatic quaternary ammonium, phosphonium and sulfonium compounds in which the aliphatic moieties can be straight or branched chain, and wherein one of the aliphatic substituents contains from about 8 to 18 carbon atoms and one contains an anionic water-solubilizing group.

The instant granular compositions can also comprise those detergency builders commonly taught for use in laundry compositions. Useful builders herein include any of the conventional inorganic and organic water-soluble builder salts, as well as various water-insoluble and so-called "seeded" builders.

Inorganic detergency builders useful herein include, for example, water-soluble salts of phosphates, pyrophosphates, orthophosphates, polyphosphates, phosphonates, carbonates, bicarbonates, borates and silicates. Specific examples of inorganic phosphate builders include sodium and potassium tripolyphosphates, pyrophosphates, and hexametaphosphates. The polyphosphonates specifically include, for example, the sodium and potassium salts of ethane 1-hydroxy-1,1-diphosphonic acid, and the sodium and potassium salts of ethane-1,1,2-triphosphonic acid. Examples of these and other phosphorus builder compounds are disclosed in U.S. Pat. Nos. 3,159,581; 3,213,030; 3,422,021; 3,422,137; 3,400,176 and 3,400,148; incorporated herein by reference. Sodium tripolyphosphate is an especially preferred, water-soluble inorganic builder herein.

Non-phosphorus containing sequestrants can also be selected for use herein as detergency builders. Specific examples of non-phosphorus, inorganic builder ingredients include water-soluble inorganic carbonate, bicarbonate, borate and silicate salts.

Water-soluble, organic builders are also useful herein. For example, the alkali metal, ammonium and substituted ammonium polyacetates, polyacetal carboxylates, carboxylates, polycarboxylates, succinates, and polyhydroxysulfonates are useful builders in the present compositions and processes. Specific examples of the polyacetate and polycarboxylate builder salts include sodium, potassium, lithium, ammonium and substituted ammonium salts of ethylene diamine tetraacetic acid, nitrilotriacetic acid, oxydisuccinic acid, mellitic acid, benzene polycarboxylic acids, and citric acid.

Highly preferred non-phosphorus builder materials (both organic and inorganic) herein include sodium carbonate, sodium bicarbonate, sodium silicate, sodium citrate, sodium oxydisuccinate, sodium mellitate, sodium nitrilotriacetate, and sodium ethylenediaminetetraacetate, and mixtures thereof.

Another type of detergency builder material useful in the present compositions and processes comprises a water-soluble material capable of forming a water-insoluble reaction product with water hardness cations in combination with a crystallization seed which is capable of providing growth sites for said reaction product.

Specific examples of materials capable of forming the water-insoluble reaction product include the water-soluble salts of carbonates, bicarbonates, sesquicarbonates, silicates, aluminates and oxalates. The alkali metal, especially sodium, salts of the foregoing materials are preferred for convenience and economy.

Another type of builder useful herein includes various substantially water-insoluble materials which are capable of reducing the hardness content of laundering liquors, e.g., by ion-exchange processes. Examples of such builder materials include the phosphorylated cloths disclosed in U.S. Pat. No. 3,424,545, Bauman, issued Jan. 28, 1969, incorporated herein by reference.

The complex aluminosilicates, i.e., zeolite-type materials, are useful presoaking/washing adjuvants herein in that these materials soften water, i.e., remove Ca++ hardness. Both the naturally occurring and synthetic "zeolites", especially zeolite A and hydrated zeolite A materials, are useful for this builder/softener purpose. A description of zeolite materials and a method of preparation appears in Milton, U.S. Pat. No. 2,882,243, issued Apr. 14, 1959, incorporated herein by reference.

Bleaching compositions of this invention are normally solid thereby facilitating preparation of detergent compositions. The novel bleaches of this invention can be admixed with other granules of optional bleaching or detergent composition materials. Actual particle size of either the bleach-containing granules or optional granules of additional material is not critical. If, however, compositions are to be realized having commercially acceptable flow properties, certain granule size limitations are highly preferred. In general, all granules of the instant compositions preferably range in size from about 100 microns to 3000 microns, more preferably from about 100 microns to 1300 microns.

Additionally, flowability is enhanced if particles of the present invention are of approximately the same size. Therefore, preferably the ratio of the average particle sizes of the bleach-containing granules and optional granules of other materials varies between 0.5:1 and 2.0:1.

Bleaching compositions of the present invention are utilized by dissolving them in water in an amount sufficient to provide from about 1.0 ppm to 50 ppm available oxygen in solution. Generally, this amounts to about 0.0001% to 0.005% by weight of active oxygen in solution. Fabrics to be bleached are then contacted with such aqueous bleaching solutions.

Among the sulfone peroxycarboxylic acids of this invention, the degree of bleaching activity per unit weight of active oxygen can vary widely. Preferred embodiments are those with a relatively high level of bleaching activity per unit weight of active oxygen, since smaller amounts of such compounds can be used to achieve a given degree of bleaching. Embodiments which sustain this high performance at relatively low bleaching temperatures, i.e. .ltoreq.60.degree. C. are particularly preferred. Also preferred are embodiments with a relatively high weight percentage of active oxygen in the sulfone peroxycarboxylic acid molecule, since such embodiments tend to consume a smaller weight of raw materials per unit of active oxygen present.

Thermal and moisture stability of the peroxyacid bleaches are important for safety, storage and shelflife considerations. Many prior art peroxycarboxylic acids that have good bleaching performance have not been commercialized due to poor thermal and moisture stability properties. However, the sulfone peroxyacids of this invention have shown surprisingly high thermal and moisture stabilities.

While the degree of molecular stability (as reflected in such properties as storage stability or thermal stability in various formulations, etc.) will vary among sulfone peroxycarboxylic acids, they are usually more stable than otherwise similar peroxycarboxylic acids which lack the sulfone group. Similarly the tendency to cause dye damage will vary but will usually be reduced by the presence of one or more sulfone groups. Preferred embodiments are those exhibiting relatively high degrees of stability and relatively low degrees of dye damage. Particularly preferred are embodiments which exhibit in a single molecule or reaction product a combination of high stability, low dye damage, and high bleaching activity per unit weight.

Depending upon the specific intended use, such properties as particle size, appearance, and odor of the sulfone peroxycarboxylic acids of this invention may be important. In most embodiments, these compounds can be produced as white, relatively odorless powders of relatively small particle size, and such embodiments are usually preferred. If desired, particle size distribution can be adjusted by such known methods as milling, screening, or agglomeration.

Included within the scope of this invention are various bleaching processes in which sulfone peroxycarboxylic acids are employed in effective amounts as active bleaching ingredients. Generally, in such processes, articles to be bleached are contacted in an aqueous medium with a bleach effective amount of one or more sulfone peroxycarboxylic acids. Other conditions important in such processes include temperature, pH, contact time, selection and level of various ingredients present during bleaching, agitation, etc. Optimization of such conditions can be accomplished for each particular case by routine experimentation in view of this disclosure. Particularly preferred are processes in which the temperature is fairly low, i.e. not above 60.degree. C., since such processes provide rapid and effective bleaching while minimizing adverse effects associated with higher temperatures such as dye damage, fabric shrinkage, high energy consumption, and weakening of fabrics or other articles subjected to bleaching.

Although the invention has been described in terms of specific embodiments which are set forth in considerable detail, it should be understood that this description is by way of illustration only and that the invention is not necessarily limited thereto since alternative embodiments and operating techniques will become apparent to those skilled in the art in view of this disclosure. Accordingly, modifications are contemplated which can be made without departing from the spirit of the described invention.