Phosphate buffer wash for improved amidoperoxyacid storage stability.

TECHNICAL FIELD

This invention relates to a process for improving the storage stability of an amidoperoxyacid, comprising contacting said amidoperoxyacid with a phosphate buffer solution at a pH between about 3.5 and 6 after synthesis of the amidoperoxyacid and before its incorporation into a final product. Chelants can optionally be added to the buffer to further improve the storage stability of the amidoperoxyacid.

BACKGROUND OF THE INVENTION

Organic peroxyacids are useful as fabric bleaching agents but are highly reactive compounds of limited storage stability. Storage stability refers to the extent to which the available oxygen (AvO) content of the peroxyacid is maintained over time.

Heretofore, generally three ways of improving storage stability of peroxyacids have been employed: chelants, pH control, and moisture control. The chelants combine with any metal ions present and thus prevent any decomposition of the peroxyacid which would be catalyzed by heavy metals. Seven references are representative: U.S. Patent 4,170,453, Kitko, issued October 9, 1979; U.S. Patent 4,091,544, Hutchins, issued May 30, 1978; U.S. Patent 4,100,095, Hutchins et al., issued July 11, 1978; U.S. Patent 4,126,573, Johnston, issued November 21, 1978; U.S. Patent 4,259,201, Cockrell, Jr. et al., issued March 31, 1981; U.S. Patent 4,325,828, Postlethwaite, issued April 20, 1982; and European Patent Application 0068547, Bossu et al., filed June 9, 1982.

The preferred chelating stabilization system in these references is a mixture of 8-hydroxyquinoline or dipicolinic acid and an acid polyphosphate. Although chelants reduce or eliminate the problem of decomposition caused by heavy metals, they do not address the problem of decomposition of acid-sensitive peroxyacids caused by the acidic environment remaining after synthesis of the peroxyacid.

Several references suggest pH control as a way to optimize stability of bleach and/or detergent compositions. See European Patent Application 0176124, de Jong et al., published April 2, 1986 (pH 3.5-4.5); European Patent Application 0201958, Meijer et al., published November 20, 1986 (pH 4.1); U.S. Patent 4,287,135, Stober et al., issued September 1, 1981 (pH 2-6 and coating with reaction mixture); and European Patent Application 0200163, Jacobs et al., published November 5, 1986 (pH 3-7). The last reference also includes a polymer coating of the bleach granule. All of these references except Stober et al. also include chelants.

European Patent Application 0212976, Coyne et al., published March 4, 1987 teaches improved peracid stability through control of water levels during synthesis of peracid.

With an acid-sensitive peroxyacid such as an amidoperoxyacid, it is especially important that a way be found to make the peroxyacid stable for storage. Otherwise, the amidoperoxyacid, even with known storage stabilizers such as those described above, will decompose over time. It has been found that contacting the amidoperoxyacid with phosphate buffer at a pH between about 3.5 and 6, preferably between about 4 and 5, just after synthesis of the amidoperoxyacid, significantly slows this decomposition. Although this process is simple, it has heretofore not been used to stabilize peroxyacid. The amidoperoxyacid washed in phosphate buffer remains stable even when incorporated into an alkaline detergent composition, which is also surprising.

Amidoperoxyacids, or peroxyacids with a polar amide link in the hydrophobic chain, are described in U.S. Patent 4,634,551, Burns et al., issued January 6, 1987, and U.S. Patent 4,686,063, Burns, issued August 11, 1987. Such amidoperoxyacids have the following general formulas: <chemistry id="chem0001" num="0001"><img file="EP0349220A2_D0001.tif" /></chemistry> wherein R¹ and R² are alkyl(ene), aryl(ene) or alkaryl(ene) groups containing from about 1 to about 14 carbon atoms and R⁵ is H or an alkyl, aryl, or alkaryl group containing from about 1 to about 10 carbon atoms.

Sulfone peroxyacids, which are generally more stable than amidoperoxyacids, are represented by the following formula: <chemistry id="chem0002" num="0002"><img file="EP0349220A2_D0002.tif" /></chemistry> wherein A and B are organic moieties bonded to the sulfur atom by a carbon atom and at least one of A and B containing at least one - <img file="EP0349220A2_D0003.tif" /> - OOH group bonded to a carbon atom. Sulfone peroxyacids are disclosed in European Patent Application 0267175, Dyroff et al., published May 11, 1988. In Example 4 of that application a methylene chloride solution of the sulfone peroxyacid was washed with phosphate buffer solution, then washed with water, partially evaporated and mixed with boric acid as a part of a series of steps.

It is an object of the present invention to provide a means of improving the storage stability of amidoperoxyacids.

It is also an object of the present invention to provide a means of improving amidoperoxyacid storage stability in a detergent composition.

SUMMARY OF THE INVENTION

This invention relates to a process for improving the storage stability of an amidoperoxyacid, comprising contacting said amidoperoxyacid with a phosphate buffer solution at a pH between about 3.5 and 6 after synthesis of the amidoperoxyacid and before its incorporation into a final product. Chelants can optionally be added to the buffer to further improve the storage stability of the amidoperoxyacid.

DETAILED DESCRIPTION OF THE INVENTION

Amidoperoxyacids are synthesized, then contacted with phosphate buffer solution at a pH between about 3.5 and 6, preferably between about 4 and 5. Conventional stabilizers known in the art can be, and preferably are, also employed. The stabilized amidoperoxyacid can then be agglomerated for use in a detergent composition or as a bleaching agent.

Amidoperoxyacids, or peroxyacids with a polar amide link in the hydrophobic chain, are described in U.S. Patent 4,634,551, Burns et al., issued January 6, 1987, and U.S. Patent 4,686,063, Burns, issued August 11, 1987, both incorporated herein by reference.

Amidoperoxyacids herein have the following general formulas: <chemistry id="chem0003" num="0003"><img file="EP0349220A2_D0004.tif" /></chemistry> wherein R¹ and R² are alkyl(ene), aryl(ene) or alkaryl(ene) groups containing from about 1 to about 14 carbon atoms and R⁵ is H or an alkyl, aryl, or alkaryl group containing from about 1 to about 10 carbon atoms. Preferred amidoperoxyacids are those having the following general formula: R¹ - NH - <img file="EP0349220A2_D0005.tif" /> - R² - <img file="EP0349220A2_D0006.tif" /> - OOH wherein R¹ is an alkyl group containing from about 6 to about 12 carbon atoms, and R² is an alkyl containing from 1 to about 6 carbon atoms.

The amidoperoxyacids most preferred herein are the mono<u style="single">n</u>onyl­<u style="single">a</u>mide of <u style="single">p</u>eroxy<u style="single">s</u>uccinic <u style="single">a</u>cid ("NAPSA") and the mono<u style="single">n</u>onyl<u style="single">a</u>mide of <u style="single">p</u>eroxy<u style="single">a</u>dipic <u style="single">a</u>cid ("NAPAA"). Example I of U.S. Patent 4,686,063 contains a description of the synthesis of NAPSA, from column 8, line 40 to Column 9, line 5, and NAPAA, from column 9, line 15 to column 9, line 65.

At the end of the amidoperoxyacid synthesis, the reaction is quenched with water, filtered, washed with water to remove some excess sulfuric acid (or other strong acid with which the peroxyacid was made), and filtered again.

The amidoperoxyacid wet cake thus obtained is contacted with a phosphate buffer solution at a pH between about 3.5 and 6, preferably between about 4 and 5. It has been found that if the pH of the amidoperoxyacid wet cake is raised too high, the amidoperoxyacid is dissolved, but if the pH is too low, the amidoperoxyacid is unstable. Without meaning to be bound by theory, it is believed that to stabilize the amidoperoxyacid, the strong acidity remaining from the sulfuric acid (or other strong acid) with which the peroxyacid is made must be neutralized without at the same time destroying the weak acid which is the peroxyacid. A buffer accomplishes this purpose. It has been determined that phosphate buffer, but not acetate or water washing, stabilizes the amidoperoxyacid. Since water washing to the same pH does not achieve the same effect as the phosphate buffer wash, it is theorized that some of the phosphate remains in the wet cake after contact with the phosphate buffer, which also helps storage stability. This is further borne out by the fact that phosphate buffer washing followed by water washing results in the peroxyacid having less stability than phosphate buffer washing alone.

The phosphate buffer is preferably orthophosphate or pyrophosphate in a concentration range of from about 0.01 M (moles/liter) to about 1 M. Most preferred is a 0.10 M solution of orthophosphates. These can be selected from the group consisting of H₃PO₄ (phosphoric acid), NaH₂PO₄ (monobasic sodium phosphate), Na₂HPO₄ (dibasic sodium phosphate), and Na₃PO₄ (tribasic sodium phosphate), so that the final solution has a pH of between about 3.5 and 6, preferably between about 4 and 5. Other salts such as potassium can be employed. Examples of phosphate buffer solution compositions can be found in <u style="single">Buffers for pH and Metal Ion Control</u> by D.D. Perrin and Boyd Dempsey (Chapman &amp; Hall, 1974).

There are several ways that the amidoperoxyacid can be contacted with the phosphate buffer solution. Preferably, the amidoperoxyacid wet cake is placed in enough of the phosphate buffer to cover it, and the combination is slowly stirred for a period of time sufficient to assure thorough contact with the wet cake. Approximately one hour for 20.0 g of wet cake in 400 ml of phosphate buffer (0.10 M, pH=4.75), for example, is an appropriate amount of time. Suction filtration is then preferably applied to remove the solution. The wet cake can then be air dried overnight. Conceivably, less phosphate buffer solution of a stronger concentration could be used. A 0.1 M phosphate buffer solution is preferred since it provides more volume and, when mixed with the wet cake, thorough contact and easier stirring than, for example, a 0.5 M solution.

Another preferred way of contacting the wet cake with the buffer is to pour the buffer over the wet cake and then apply vacuum filtration. In a plant, the filtered wet cake could be placed on a fluid bed for final drying before it is incorporated into the final detergent composition or bleaching agent.

The phosphate buffer wash should be done before the amidoperoxyacid has decomposed. The product has decomposed when there is so little amidoperoxyacid remaining that it is no longer an effective bleach. The activity of the amidoperoxyacid can be measured by the available oxygen. Generally, the higher the AvO is, the better the peroxyacid will bleach.

Other agents for storage stabilization or exotherm control can be added to the amidoperoxyacid before incorporation into the final product. It is preferred that boric acid, an exotherm control agent disclosed in U.S. Patent 4,686,063, Burns, issued August 11, 1987 and incorporated herein, be mixed with the preferred NAPSA (which has been washed in phosphate buffer) in about a 2:1 NAPSA:boric acid ratio. It is also preferred that the phosphate buffer washed NAPSA be mixed with appropriate amounts of dipicolinic acid and tetrasodium pyrophosphate, a chelating stabilization system (see Background section above). It is preferred that this mixture be formed into granules, dried, and used either separately or as part of a granular detergent composition.

The granules can be comprised of from about 1% to about 50% of the phosphate buffer washed amidoperoxyacid, preferably from about 10% to about 30% of NAPSA or NAPAA; from about 0.5% to about 25% of an exotherm control agent, preferably from about 5% to about 15% of boric acid; from 0 to about 10% of C₁₁₋₁₃ linear alkylbenzene sulfonate or C₁₄₋₁₅ alkyl sulfate, preferably from about 2% to about 7% of C₁₁₋₁₃ linear alkylbenzene sulfonate; from about 20% to about 70%, preferably from about 40% to about 60%, sulfate; and from 0 to about 20% of a chelating agent, preferably from about 0.02% to about 0.10% tetrasodium pyrophosphate and from about 0.05% to about 0.20% of dipicolinic acid.

Chelants can optionally be included in the phosphate buffer before contact with the wet cake. Without wishing to be bound by theory, it may be that adding the chelants in this way improves their effectiveness by more evenly distributing the chelants throughout the wet cake.

Examples of suitable chelants for use herein are: carboxylates, such as ethylene diamine tetraacetate (EDTA) and diethylene triamine pentaacetate (DTPA); polyphosphates, such as sodium acid pyrophosphate (SAPP), tetrasodium pyrophosphate (TSPP), and sodium tripolyphosphate (STPP); phosphonates, such as ethylhydroxydiphosphonate (Dequest® 2010) and other sequestering agents sold under the Dequest® trade name; and combinations of the above. Other sequestering agents for use herein are dipicolinic acid, picolinic acid, and 8-hydroxyquinoline, and combinations thereof.

It is preferred that the amidoperoxyacid washed in phosphate buffer be used in a detergent composition or as a separate bleaching agent. It is more preferred that the phosphate buffer washed amidoperoxyacid be incorporated into a granular detergent composition. It is most preferred that the amidoperoxyacid be NAPSA or NAPAA and be formed into granules (after the phosphate buffer wash and drying) which are then incorporated into a granular detergent composition.

Such detergent compositions comprise from about 0.5% to about 30%, preferably from about 1% to about 10%, of the amidoperoxy­acid; from about 1% to about 40%, preferably from about 2% to about 30%, of detergent surfactants; and from about 5% to about 80%, preferably from about 10% to about 60%, of detergency builder. These detergent compositions can include any or all of the ingredients set forth in U.S. Patent 3,936,537, Baskerville et al, incorporated herein by reference. Such components include color speckles, suds boosters, suds suppressors, antitarnish and/or anticorrosion agents, soil-suspending agents, soil-release agents, dyes, fillers, optical brighteners, germicides, alkalinity sources, hydrotropes, antioxidants, enzymes, enzyme stabilizing agents, perfumes, etc.

Appropriate ingredients are described in U.S. Patent 4,686,063, column 4, line 4 to column 8, line 33, and U.S. Patent 4,634,551, column 7, line 3 to column 11, line 33.

NAPSA which has been washed in phosphate buffer, filtered, granulated with boric acid and chelants, and incorporated into a granular detergent composition has significantly more available oxygen over time in product when compared to a control not washed in phosphate buffer (see Example II). This indicates that washing with phosphate buffer significantly improves amidoperoxyacid storage stability in a detergent composition.

The following examples are given to illustrate the parameters of and compositions within the invention. All percentages, parts and ratios are by weight unless otherwise indicated.

EXAMPLE 1

A freshly-prepared sample of NAPSA (monononylamide of peroxysuccinic acid) wet cake was obtained which consisted of 56.7% water, 2.12% available oxygen (corresponding to 34.4% peroxyacid), and the rest (9.1%) unreacted starting material. This wet cake was the crude reaction product of NASA (mono<u style="single">n</u>onyl<u style="single">a</u>mide of <u style="single">s</u>uccinic <u style="single">a</u>cid), sulfuric acid, and hydrogen peroxide which was subsequently quenched by addition to water followed by filtration, washing with distilled water, and final suction filtration to recover the wet cake. A 10% weight volume (w/v) slurry of wet cake (10 g wet cake solids in 100 ml of distilled water) had a pH of 3.15. Portions of the wet cake were then subjected to the following treatments. Phosphate buffers were made by mixing 0.10 M (moles/liter) solutions of NaH₂PO₄, Na₂HPO₄, and Na₃PO₄ to achieve the desired pH. <ul id="ul0001" list-style="none"><li><u style="single">Sample #1</u> 20.0 g of wet cake was air-dried overnight at room temperature. When dry, the sample pH (as a 10% w/v slurry in distilled water) was 2.96.</li><li><u style="single">Sample #2</u> 15.0 g of wet cake was washed with 1.0 liter of distilled water and then air-dried overnight at room temperature. When dry, the sample pH was 4.60.</li><li><u style="single">Sample #3</u> 20.0 g of wet cake was washed with 1.0 liter of phosphate buffer (0.10 M, pH=4.40) followed by 1.0 liter of distilled water and then air-dried overnight at room temperature. When dry, the sample pH was 4.59.</li><li><u style="single">Sample #4</u> 15.0 g of wet cake was washed with 1.0 liter of phosphate buffer (0.10 M, pH=4.50) and then air-dried overnight at room temperature. When dry, the sample pH was 4.49.</li><li><u style="single">Sample #5</u> 20.0 g of wet cake was placed in 400 ml of phosphate buffer (0.10 M, pH=4.75) and stirred for 1 hour after which it was recovered by suction filtration and air-dried overnight. When dry, the sample pH was 4.76.</li></ul>

The NAPSA samples were placed in open containers for storage stability testing at 80^oF (26.7^oC), 100^oF (37.8^oC), and 120^oF (48.9^oC). Stability was monitored by iodometric titration with sodium thiosulfate. Results are expressed below in terms of percent peroxyacid available oxygen (AvO) remaining as a function of time. <tables id="tabl0001" num="0001"><table frame="all"><tgroup cols="4" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="39.37mm" /><colspec colnum="2" colname="col2" colwidth="39.37mm" /><colspec colnum="3" colname="col3" colwidth="39.37mm" /><colspec colnum="4" colname="col4" colwidth="39.37mm" /><thead valign="top"><row><entry namest="col1" nameend="col1" align="center"><u style="single">Sample #</u></entry><entry namest="col2" nameend="col2" align="center"><u style="single">Wash</u></entry><entry namest="col3" nameend="col3" align="center"><u style="single">Temperature</u></entry><entry namest="col4" nameend="col4" align="center"><u style="single">Percent of Initial AvO Remaining After 12 Weeks</u></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">1</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">None</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">40</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">37</entry></row><row rowsep="1"><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">2</entry></row><row><entry namest="col1" nameend="col1" morerows="2" align="right">2</entry><entry namest="col2" nameend="col2" morerows="2" align="left">Water</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">94</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">92</entry></row><row><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">43</entry></row><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">3</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">Phosphate buffer then water</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">100</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">99</entry></row><row rowsep="1"><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">70</entry></row><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">4</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">Phosphate buffer</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">99</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">100</entry></row><row rowsep="1"><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">97</entry></row><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">5</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">Phosphate buffer-soaked</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">98</entry></row><row><entry namest="col1" nameend="col1" align="right">100°F</entry><entry namest="col2" nameend="col2" align="right">98</entry><entry namest="col3" nameend="col3" /><entry namest="col4" nameend="col4" /></row><row rowsep="1"><entry namest="col1" nameend="col1" align="right">120°F</entry><entry namest="col2" nameend="col2" align="right">96</entry><entry namest="col3" nameend="col3" /><entry namest="col4" nameend="col4" /></row></tbody></tgroup></table></tables>

Phosphate buffer stabilization of the peroxyacid does not occur only as the result of raising the wet cake pH. Washing the wet cake to a similar pH with water resulted in less stability after 12 weeks at 120^oF than when the phosphate buffer wash treatment was used (Sample #2 vs. Sample #4). Part of the beneficial effect of the phosphate buffer upon stability is apparently derived from residual amounts of buffer left in the peroxyacid wet cake after washing. Buffer washing followed by water washing resulted in peroxyacid having less stability than peroxyacid washed with buffer alone (Sample #3 vs. Sample #4).

EXAMPLE II

This example shows the improved storage stability of an amidoperoxyacid washed in phosphate buffer, filtered, granulated, and incorporated into a granular detergent composition.

<u style="single">Sample #1</u> of granulated NAPSA was prepared by combining the following: <tables id="tabl0002" num="0002"><table frame="all"><tgroup cols="3" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="52.50mm" /><colspec colnum="2" colname="col2" colwidth="52.50mm" /><colspec colnum="3" colname="col3" colwidth="52.50mm" /><tbody valign="top"><row><entry namest="col1" nameend="col1" align="char" char=".">80.00</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">dried NAPSA wet cake (described in Example I)</entry></row><row><entry namest="col1" nameend="col1" align="char" char=".">31.31</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">boric acid</entry></row><row><entry namest="col1" nameend="col1" align="char" char=".">25.05</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">C13 linear alkylbenzene sulfonate paste</entry></row><row><entry namest="col1" nameend="col1" align="char" char=".">0.30</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">dipicolinic acid</entry></row><row><entry namest="col1" nameend="col1" align="char" char=".">0.15</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">tetrasodium pyrophosphate</entry></row><row><entry namest="col1" nameend="col1" align="char" char=".">123.58</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">sodium sulfate</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="char" char=".">45.00</entry><entry namest="col2" nameend="col2" align="left">g</entry><entry namest="col3" nameend="col3" align="left">water</entry></row></tbody></tgroup></table></tables>

All ingredients were thoroughly mixed and then the granules were formed by passing the mixture through a #18 Tyler mesh plastic sieve followed by air-drying overnight at room temperature. When dry, the granules prepared in this manner had a pH=4.21 (measured as a 10% weight volume slurry in distilled water).

<u style="single">Sample #2</u> of granulated NAPSA was prepared by combining all of the same ingredients in identical proportions with the exception that the NAPSA wet cake was first subjected to phosphate buffer treatment. 50.0 g of wet cake was added to a 1.0 liter of phosphate buffer (0.10 M, pH=4.75) and then stirred for 1 hour after which the NAPSA wet cake was recovered by suction filtration. Granulation was then carried out as for Sample #1. Sample #2 had a pH=4.23 after drying.

Portions of the granulated peroxyacid samples (16%) were combined with a phosphate detergent granule (84%) and placed in open containers at 80^oF (26.7^oC), 100^oF (37.8^oC), and 120^oF (48.9^oC) for storage stability testing.

The composition of the spray-dried phosphate detergent granule was: <tables id="tabl0003" num="0003"><table frame="all"><tgroup cols="2" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><thead valign="top"><row><entry namest="col1" nameend="col1" /><entry namest="col2" nameend="col2" align="center"><u style="single">Weight %</u></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">C₁₁-₁₃ linear alkylbenzene sulfonate</entry><entry namest="col2" nameend="col2" align="right">11</entry></row><row><entry namest="col1" nameend="col1" align="left">C₁₄-₁₅ alkyl sulfate</entry><entry namest="col2" nameend="col2" align="right">11</entry></row><row><entry namest="col1" nameend="col1" align="left">C₁₂-₁₃ alkyl ethoxylate (6.5)*</entry><entry namest="col2" nameend="col2" align="right">1</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium tripolyphosphate</entry><entry namest="col2" nameend="col2" align="right">36</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium pyrophosphate and sodium acid pyrophosphate</entry><entry namest="col2" nameend="col2" align="right">9</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium silicate (2.0 ratio)</entry><entry namest="col2" nameend="col2" align="right">4</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium sulfate, moisture, and miscellaneous</entry><entry namest="col2" nameend="col2" align="right">28</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Total</entry><entry namest="col2" nameend="col2" align="right">100</entry></row></tbody></tgroup><tgroup cols="2" colsep="0" rowsep="0"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><tbody valign="top"><row><entry namest="col1" nameend="col2" align="justify">*Alcohol and monoethoxylated alcohol removed.</entry></row></tbody></tgroup></table></tables>

Results are expressed below in terms of percent peroxyacid available oxygen (AvO) remaining as a function of time. <tables id="tabl0004" num="0004"><table frame="all"><tgroup cols="4" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="39.37mm" /><colspec colnum="2" colname="col2" colwidth="39.37mm" /><colspec colnum="3" colname="col3" colwidth="39.37mm" /><colspec colnum="4" colname="col4" colwidth="39.37mm" /><thead valign="top"><row><entry namest="col1" nameend="col1" align="center"><u style="single">Sample #</u></entry><entry namest="col2" nameend="col2" align="center"><u style="single">Wash</u></entry><entry namest="col3" nameend="col3" align="center"><u style="single">Temperature</u></entry><entry namest="col4" nameend="col4" align="center"><u style="single">Percent of Initial AvO Remaining After 12 Weeks</u></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">1</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">None</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">97</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">95</entry></row><row rowsep="1"><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">8</entry></row><row><entry namest="col1" nameend="col1" morerows="2" rowsep="1" align="right">2</entry><entry namest="col2" nameend="col2" morerows="2" rowsep="1" align="left">Phosphate buffer</entry><entry namest="col3" nameend="col3" align="right">80°F</entry><entry namest="col4" nameend="col4" align="right">97</entry></row><row><entry namest="col3" nameend="col3" align="right">100°F</entry><entry namest="col4" nameend="col4" align="right">94</entry></row><row rowsep="1"><entry namest="col3" nameend="col3" align="right">120°F</entry><entry namest="col4" nameend="col4" align="right">60</entry></row></tbody></tgroup></table></tables>

Thus the buffer treatment can increase in-product peroxyacid stability even when used in conjunction with other stabilizers such as dipicolinic acid and tetrasodium pyrophosphate.

EXAMPLE III

Wet cake containing the mono<u style="single">n</u>onyl<u style="single">a</u>mide of <u style="single">p</u>eroxy<u style="single">a</u>dipic <u style="single">a</u>cid (NAPAA) is prepared in the following manner. A weight of 50.0 g of the methyl ester of 6-nonylamino-6-oxocaproic acid is dissolved in 100 ml of methanesulfonic acid and the resulting solution is cooled in an ice bath. While stirring, 42.4 g of 70% H₂O₂ are added dropwise at a rate such that the temperature of the reaction mixture does not rise above 20^oC. After addition of the H₂O₂ is complete, the ice bath is removed and the reaction mixture is cooled in a freezer and then poured over ice. The solid reaction product is recovered as wet cake by filtration followed by water washing and final suction filtration. The wet cake is stabilized by addition to pyrophosphate buffer stabilizing solution in the ratio: 50 g wet cake/1 .0 liter of solution. The pyrophosphate solution is 0.10 M, pH=5.00 (21.10 g Na₂H₂P₂O₇ + 1.38 g Na₄P₂O₇ + 0.10 g Dequest® 2010 per liter) after which it is stirred for 15 minutes to 1 hour and recovered by suction filtration. The stabilized peroxyacid wet cake can then be dried or granulated.

EXAMPLE IV

50.0 g of NAPSA wet cake made as described in Example I above is stabilized by addition to 1 liter of phosphate buffer (0.10 M, pH=4.50), stirred for 1 hour, then recovered by suction filtration. The NAPSA is granulated by combining the stabilized wet cake with the following granule ingredients. <tables id="tabl0005" num="0005"><table frame="all"><tgroup cols="2" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><thead valign="top"><row><entry namest="col1" nameend="col1" /><entry namest="col2" nameend="col2" align="center"><u style="single">Weight %</u></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">NAPSA (solids)</entry><entry namest="col2" nameend="col2" align="char" char=".">24.00</entry></row><row><entry namest="col1" nameend="col1" align="left">NASA (solids, from wet cake)</entry><entry namest="col2" nameend="col2" align="char" char=".">4.00</entry></row><row><entry namest="col1" nameend="col1" align="left">Boric acid</entry><entry namest="col2" nameend="col2" align="char" char=".">12.50</entry></row><row><entry namest="col1" nameend="col1" align="left">C₁₃ linear alkylbenzene sulfonate (paste)</entry><entry namest="col2" nameend="col2" align="char" char=".">5.00</entry></row><row><entry namest="col1" nameend="col1" align="left">Dipicolinic acid</entry><entry namest="col2" nameend="col2" align="char" char=".">0.12</entry></row><row><entry namest="col1" nameend="col1" align="left">Tetrasodium pyrophosphate</entry><entry namest="col2" nameend="col2" align="char" char=".">0.06</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Sodium sulfate</entry><entry namest="col2" nameend="col2" align="char" char=".">54.32</entry></row></tbody></tgroup></table></tables> The granules are formed by passage through a #18 Tyler mesh plastic sieve and are air-dried overnight.

The NAPSA granules are then admixed with a spray dried granular detergent composition to provide a finished bleach detergent composition having the following composition. <tables id="tabl0006" num="0006"><table frame="all"><tgroup cols="2" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><thead valign="top"><row><entry namest="col1" nameend="col1" /><entry namest="col2" nameend="col2" align="center"><u style="single">Weight %</u></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">C₁₁-₁₃ linear alkylbenzene sulfonate</entry><entry namest="col2" nameend="col2" align="char" char=".">8.0</entry></row><row><entry namest="col1" nameend="col1" align="left">C₁₄-₁₅ alkyl sulfate</entry><entry namest="col2" nameend="col2" align="char" char=".">8.0</entry></row><row><entry namest="col1" nameend="col1" align="left">C₁₂-₁₃ alkyl ethoxylate (6.5)*</entry><entry namest="col2" nameend="col2" align="char" char=".">0.2</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium tripolyphosphate</entry><entry namest="col2" nameend="col2" align="char" char=".">39.4</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium carbonate</entry><entry namest="col2" nameend="col2" align="char" char=".">12.3</entry></row><row><entry namest="col1" nameend="col1" align="left">Sodium silicate (1.6 ratio)</entry><entry namest="col2" nameend="col2" align="char" char=".">5.6</entry></row><row><entry namest="col1" nameend="col1" align="left">NAPSA granules</entry><entry namest="col2" nameend="col2" align="char" char=".">18.0</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Sodium sulfate, moisture, and miscellaneous</entry><entry namest="col2" nameend="col2" align="char" char=".">8.5</entry></row></tbody></tgroup><tgroup cols="2" colsep="0" rowsep="0"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><tbody valign="top"><row><entry namest="col1" nameend="col2" align="justify">*Alcohol and monoethoxylated alcohol removed.</entry></row></tbody></tgroup></table></tables>