Title of Invention	PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS SOLVENT
Abstract	A process for converting an alcohol comprising amide group to corresponding carboxylic acid in yield ≥75% which process comprises reacting: R1 - CONR2 (CH2)mOH wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6, with an oxidizing agent in the presence of a hindered nitroxide radical and optional co-catalyst, wherein the solvent is solely water and, in the presence of the oxidizing agent, oxidizing agent separates into water, and the amidoalcohol stays or partitions in a solid organic layer to thereby permit the high yields noted.

Title of Invention

PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS SOLVENT

Abstract

A process for converting an alcohol comprising amide group to corresponding carboxylic acid in yield ≥75% which process comprises reacting: R1 - CONR2 (CH2)mOH wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6, with an oxidizing agent in the presence of a hindered nitroxide radical and optional co-catalyst, wherein the solvent is solely water and, in the presence of the oxidizing agent, oxidizing agent separates into water, and the amidoalcohol stays or partitions in a solid organic layer to thereby permit the high yields noted.

Full Text	FORM - 2 THE PATENTS ACT, 1970 (39 of 1970) & The Patents Rules, 2003 COMPLETE SPECIFICATION (See Section 10 and Rule 13) PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS SOLVENT HINDUSTAN UNILEVER LIMITED, a company incorporated under the Indian Companies Act, 1913 and having its registered office at 165/166, Backbay Reclamation, Mumbai -400 020, Maharashtra, India The following specification particularly describes the invention and the manner in which it is to be performed PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS SOLVENT FIELD OF THE INVENTION The present invention relates to a process for converting a compound or polymer comprising a primary alcohol and an amide group to amidocarboxylic acid. In particular, the primary amido alcohol is converted to carboxylic acid in unexpectedly high yields when proper solvent (e.g., water) is selected. In addition, when chlorine or chlorinated molecules are used as oxidizing agents, specific processing parameters used in one embodiment of the invention ensure that chlorinated amido nitrogen is not formed. BACKGROUND Amidocarboxylic acids are desirable surfactants in that they have good water solubility, good detergency and foaming properties and are mild to skin and hair. One method for the production of such surfactant is through the oxidation of an alcohol containing an amide group (e.g., coco mono-ethanolamide or CMEA). The problem, however, is that it is very difficult to drive the oxidation of alcohol to carboxylic acid efficiently. The reaction will often stop at the aldehyde stage, and the yields of carboxylic acid as final products are qvite low. Japanese Patent Laid-open No. 05/194,334 (Sandoz) discloses a process in which a hydroxyl containing compound (which may be, for example, alkyl amide polyoxyalkanol) is made to react with at least an equimolar amount of inorganic or organic halogen-containing oxidizing agent, e.g. NaOCl, in the presence of weak base and a catalytic amount of hindered nitroxide as exemplified by 2, 2, 6, 6- tetramethylpiperidine 1-oxyl, hereafter abbreviated TEMPO, and chemical derivatives thereof. In this patent, no yield or purity information is given. The process disclosed is limited to alcohols which have polyethylene glycol or polypropylene glycol substitution, or to polyglucosides, as starting reactants. Such compounds are water-soluble or water-dispersible, which makes possible the use of water as the solvent. The patent does not teach a process using hydrophobic primary alcohols (i.e., amido alcohols) of the invention as starting reactant. Japanese Patent Laid Open No. 04/283,537 (Shell) discloses a process using an oxidizing agent such as sodium hypochlorite in the presence of TEMPO. The process relates to production of an alkoxyalkanoic acid from the corresponding alkoxyalkanol, however, and not to the production of an amidecarboxylic acid from an alcohol having an amide group. Japanese Laid Open No. 10/087,554 (Lion Corporation) discloses a process for production of amidocarboxylic acid from alcohol having an amide group using an oxidizing agent of chlorine type (e.g. NaOCl) in the presence of a nitroxide radical (e.g., TEMPO) and further in the presence of alkali metal halide or alkali earth metal halide (e.g., potassium chloride). In Examples 3 and 5, for example, an alcohol comprising amide; a nitroxide radical; and a 10% solution of alkali metal chloride (potassium or sodium bromide) in water, additional water, and acetonitrile (solvent) are charged into a beaker and stirred. Under these conditions, the acetonitrile and water mix together to form a single liquid phase. In each example, the purity of the carboxylic acid is calculated from the acid value, but nothing is stated about yield. The acid value is not selective for the desired carboxylic acid, but would include all acid components present. Unexpectedly, applicants have now found that the type of solvent or solvents used during the oxidation reaction is critical to the yield of product (carboxylic acid). Without wishing to be bound by theory, applicants believe the starting amidoalcohol must not be in the same phase as the oxidizing agent. Applicants have found that this separation of oxidizing agent and alcohol can be accomplished in at least two different ways. According to a separate application applicants have filed on same date as the subject application, the final product (e.g., amidocarboxylic acid) is partitioned into an organic solvent (i.e., using solvent that will form both a hydrophobic liquid phase and an aqueous liquid phase, rather than forming one substantially aqueous phase). In this manner, the exposed amide group on the amidoalcohol is protected from cleavage (e.g., the bleach which has partitioned mainly into aqueous phase will not attack the amidoalcohol in the separate phase), and consequently far greater yield of amidocarboxylic acid is produced. That is, it is important that, in the presence of the oxidizing agent, both a solvent rich layer (substantially free of oxidising agent) and an aqueous layer {comprising substantially of the oxidizing agent) form. In a second embodiment, which is claimed in the subject application, the oxidizing agent and the alcohol are also maintained in separate phases. Here, however, the two phases are a water phase and a solid phase, and water alone is used as the solvent. That is, the amidoalcohol, which is hydrophobic, does not dissolve or disperse into the aqueous phase (rather it stays in the solid, non-aqueous phase) while the NaOCl remains in the continuous aqueous phase. In a preferred aspect of this embodiment (water as solvent), when chlorine or chlorinated molecule (e.g., NaOCl) is used as oxidizing agent, specific process steps (i.e., heating) must be used to ensure the amido nitrogen of the final carboxylic acid is not chlorinated as this would be an undesirable by-product. As indicated, the subject application relates to processes where water is employed as solvent and, upon addition of oxidizing agent, the oxidizing agent partitions into solvent while amidoalcohol and/or amidocarboxylic acid stay in solid phase. BRIEF DESCRIPTION OF THE INVENTION The present invention provides a process for converting primary alcohol having an amide group to amidocarboxylic acid in high yield (e.g., >75, preferably >80%, more preferably >85%, more preferably ≥90% yield) which process comprises reacting a primary alcohol having amide group (amidoalcohol) with an oxidizing agent, preferably a chlorine-containing oxidant like NaOCl, in the presence of a nitroxide radical and optionally in the presence of an alkali metal halide or alkali earth metal halide. In this process the solvent in which the reaction takes place is selected such that, in the presence of the oxidizing agent, the primary amidoalcohol partitions or stays (after addition of bleach or other oxidizing agent) in the solid organic phase, while bleach or oxidizing agent partitions substantially into liquid aqueous phase. Such partitioning ensures the high yields noted above (e.g., the amide linkage is not available to be cleaved by the oxidizing agent because the oxidizing agent has partitioned into liquid aqueous phase). In other words, the amidoalcohol stays in a solid phase and oxidizing agent partitions quickly enough into the agueous phase to avoid formation of undesired by¬product. It is completely unexpected that using water as sole solvent chosen could make such critical difference. It is also a critical aspect of the invention that the catalyst used in this reaction be a hindered nitroxide radical. An optional alkali metal halide or alkali earth metal halide co-catalyst may also to be used, or the co-catalyst can be, for example, sodium tetraborate. Specifically, in one embodiment of the invention, sufficient base (e.g., sodium hydroxide) is added to the reaction to ensure reaction takes place at a pH above 6, preferably 7 to 10, more preferably 7.5 to 9, even more preferably 8 to 9. Addition of base is used to make up for consumption of oxidizing agent (e.g., sodium hypochlorite) during formation of amidocarboxylic acid. Base may be added to the oxidizing agent solution prior to addition of the oxidizing agent to the reaction or it may be added during the course of the reaction {e.g., to maintain constant pH). These and other aspects, features and advantages will become apparent to those of ordinary skill in the art from a reading of the following detailed description and the appended claims. For the avoidance of doubt, any feature of one aspect of the present invention may be utilized in any other aspect of the invention. It is noted that the examples given in the description below are intended to clarify the invention and are not intended to limit the invention to those examples per se. Other than in the experimental examples, or where otherwise indicated, all numbers expressing quantities of ingredients or reaction conditions used herein are to be understood as modified in all instances by the term "about". Similarly, all percentages are weight/weight percentages of the total composition unless otherwise indicated. Numerical ranges expressed in the format "from x to y" are understood to include x and y. When for a specific feature multiple preferred ranges are described in the format "from x to y", it is understood that all ranges combining the different endpoints are also contemplated. Where the term "comprising" is used in the specification or claims, it is not intended to exclude any terms, steps or features not specifically recited. All temperatures are in degrees Celsius (°C) unless specified otherwise. All measurements are in SI units unless specified otherwise. All documents cited are - in relevant part - incorporated herein by reference. BRIEF DESCRIPTION OF THE DRAWING Figure 1 is a liquid chromatogram (HPLC-UV-Vis) profile of products formed when reaction was carried out in CH3CN/water solvent and only a single liquid phase was formed (bottom figure, corresponding to example of JP 10/087,554 reference to Lion), compared to when solvent was THF/water and formed two liquid phases (top). In Figures 1-4, AU refers to Absorbance Units. As observed, a solvent which partitions into two liquid phases leads to high yields of N-lauroylglycine (LG) from N-lauroylmonoethanolamide (LMEA) starting material. By contrast, when the organic solvent formed a single liquid phase with the water, the yield and purity of LG (glycinate) were lower. Thus, for example, the pure LG product was predominantly formed at 13.54 minutes when two liquid phases formed but, when only one phase formed, there were huge amounts of impurities at 15.80 seconds. Figure 2 is a graph of an HPLC-UV-Vis analysis of cocoyl monoethanolamide (CMEA) oxidation to the carboxylic acid using 1.6 to 2.5 equivalents of NaOCl. Top panel is CMEA reagent before addition of NaOCl; Middle panel B is analysis of product using water process two hours after addition of NaOCl and before heating; and bottom panel C is analysis of product using the water process 24 hours after addition of NaOCl and with further heating at 80°C for 4 hours. As seen, when no heating step is used (Panel B) a C12 N-Cl glycinate intermediate is formed (i.e., between minute 22 and 23) while such chlorinated intermediate is not formed when heating step is used. Figure 3 is graph similar to Figure 2 but using 2.3 to 3.2 equivalents NaOCl to oxidize CMEA to cocoyl glycinate. Panels A again shows CMEA before addition of NaOCl, Panel B is reaction mixture 1 hour after NaOCl addition and Panel C is reaction24 hours after addition of NaOCl and further heating at 65° for 6 hours. Again, it is seen that, without heating step, C12 N-Cl glycinate intermediate is formed and such intermediate is not formed when heating step is used. Figure 4 is reaction profile of CMEA oxidation to cocoyl glycinate using 3.2 to 4.0 eq. of NaOCl. Panel A is CMEA before addition of NaOCl, Panel B is reaction 24 hours after addition of NaOCl and Panel C is mixture 24 hours after addition of NOCl and further heating at 60°C for 8 hours. Again, in absence of heating step, C12 N-Cl glycinate will form. Figure 5 is a representative total ion count spectrum of an infused cocoyl glycinate sample generated using the procedure described in Example 10. This spectrum demonstrates the absence of cocoyl N-Cl glycinate intermediate. For LC-MC analysis, a 1 mg/ml glycinate sample prepared in mobile phase was separated by HPLC and analyzed by UV and MS. A representative HPLC chromatogram with total ion count mass detection profile of a reaction aliquot from oxidation of lauroyl monoethanalamide (C12 MEA) into lauryl glycinate (C12 glycinate) is shown in Figure 6. DETAILED DESCRIPITON OF THE INVENTION The present invention relates to a novel and improved process for converting a primary alcohol comprising an amide group (e.g., C8-C22 alkoylmonoalkanolamide such as lauroyl monoethanolamide) to the corresponding amidocarboxylic acid (e.g., mixture of N-lauroyl glycine and alkalimetal N-lauroyl glycinate), and which process provides very high yields of product (e.g., ≥75%, preferably ≥ 80%, more preferably ^ 85% yield). More specifically the process comprises reacting a primary alcohol comprising such amide group with an oxidizing agent in the presence of a nitroxide radical and optional catalyst {e.g., alkali metal halide), wherein the solvent in which the reaction takes place is selected in such way that two phases separating the amidoalcohol from the oxidizing agent are formed. In other words, the amidoalcohol stays or is partitioned into an organic phase of the two phase system thereby and the oxidizing agent stays predominantly in the aqueous phase. This protects the amide group on the amidoalcohol from further cleavage and provides the high yields as noted. In the specific embodiment of the claimed invention, the amidoalcohol is separated from the oxidizing agent using only water as solvent in that the oxidizing agent partitions into the liquid aqueous water phase while the amidoalcohol stays in the undissolved solid state (heterogeneous solid- liquid system). In a preferred embodiment of this water solvent process, after addition of oxidizing agent (e.g., NaOCl), the reaction is allowed to run to completion. This generally takes 30 minutes to 24 hours, typically 1 to 10 hours. The reaction is then heated to a temperature of at least 40 up to 100°C for between 1 to 24 hours. The heating step is not necessary if non chlorine containing molecule is used in the water process because, in such case, chlorinated amido nitrogen does not form. More specifically, the starting reactant of the subject invention is an alcohol having an amide group which may be defined as follows: R2-CONR2 (CH2)m OH wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6. Examples of compounds which may be encompassed by the structure are N-alkanoylmonoethanolamines such as N-lauroylmonoethanolamide (LMEA) or N-cocoylmonoethanolamide (CMEA). The starting product may be a mixture of monoalkanolamides (e.g., monoethanolamine) including those derived from mixtures of fatty acids found in nature. N-cocoyl monoethanolamine, for example may comprise a mixture of Ca, C10 and C12 fatty acids as major component mixed with c14, C16 and C18 fatty acids. The oxidizing agent used to oxidize the starting alcohol can be any oxidizing agent which will allow the alcohol group to be oxidized to carboxylic acid. Typically, such oxidizing agents include those of the chlorine type. These may include chlorine, a hypochlorite (e.g., alkali metal hypochlorite), trichloroisocyanuric acid and dichloroisocyononic acid. Preferred oxidizing agents include sodium hypochlorite (e.g., industrial grade bleach comprises 5% to 13% sodium hypochlorite), calcium hypochlorite, chlorine itself, and organic chlorine-containing compounds, for example trichloroisocyanuric acid. Non-chlorine containing oxidants may be used, for example, oxone (2KHS05'KHS04'K2S04) , NaOBr, N-bromosuccinimide, or tribromoisocyanuric acid. Non-halogen containing antioxidants may also be used, as exemplified by H2O2, optionally in the presence of sodium tungstate dihydrate catalyst. The amount of oxidizing agent may vary, but typically eguimolar to 8 molar, preferably 1 to 7 equivalents, more preferably 2 to 6 molar are used. The starting alcohol of the invention is oxidized with an oxidizing agent (as noted above) in the presence of a hindered piperidinyloxy radical catalyst (nitroxide) and optionally in the presence of co-catalyst as are described below. The nitroxide catalyst radical used in the invention (e.g., hindered nitroxide) is produced by oxidation of a cyclic or acyclic secondary amine containing no a-hydrogens (i.e., there are no hydrogens on the carbon adjacent to N) with peroxide, or by oxidation of the corresponding hydroxylamine. Examples of stable nitroxide radicals suitable for use in this invention are mentioned in the following documents. These include linear, cyclic, dicyclic or macromolecular compounds to which one or more nitroxyl radicals are connected. Chem. Review, 78, 37 (1979): G. Rozantsev, "Free Nitroxyl Radicals", Penum Publishing Corporation, New York, 1970; and E. G. Rozantsev, V. D., Scholle, Synthesis, 1971,190. Preferred examples of the nitroxide radical are as follows. 2,2,6,6-Tetramethyl-piperidine 1-oxyl (TEMPO); 2,2,5,5-Tetramethyl-pyrrolidine 1-oxyl; and l-Aza-2,2,7,7-tetramethyl-cycloheptane 1-oxyl. TEMPO and chemical derivatives thereof are preferred, examples of which follow: 4-Hydroxyl-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Methoxy-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Ethoxy-2-2,6,6-tetramethyl-piperidine 1-oxyl; 4-Acetylamido-2-2,6,6-tetramethyl-piperidine 1-oxyl; 4-Carbamoyl-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Benzoylamino-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Oxo-2,2, 6, 6-tetramethyl-piperidine 1-oxyl; 2,2, 6, 6-Tetramethyl-piperidine-l-oxyl 4-sulfate; 2,2,6,6-Tetramethyl-piperidine-l-oxyl 4-phosphate; and 3-Carbamoyl-2,2,6,6-tetramethyl-pyrrolidine 1-oxyl. UV light stabilizers containing 2,2,6,6- tetramethylpiperidine functionality (Hindered Amine Light Stabilizers, abbreviated HALS), both monomeric and oligomeric, can serve as precursors to stable nitroxyl radicals by oxidation as well. It is also possible that an amine or a hydroxylamine which is a precursor thereof is used and, in the actual case, it is oxidized and then used. The amount of the nitroxide radical used to 1 equivalent of the starting alcohol material is typically from 0.01 to 10 mol% or, preferably, from 0.1 to 5 mol% based on amidoalcohol. An optional co-catalyst is often used with the nitroxide radical primary catalyst. The co-catalyst, if used, may be for example an alkali metal halide or alkali earth metal halide. These may include alkali metal bromide, e.g. sodium bromide, and alkali metal chloride, e.g. sodium chloride, and potassium chloride, alkali earth metal bromide, e.g. calcium bromide and magnesium bromide, alkali earth metal chloride, e.g. calcium chloride, and magnesium chloride. Typically the co-catalyst is used from 0.01 to 10 mole%, preferably 0.1 to 5 mol% equivalent based on amidoalcohol. Sodium tetraborate may be used in place of the bromide or chloride. Solvent The key to the invention resides in the selection of proper solvent, i.e., solvent which will partition into organic phase and aqueous phase upon combination of oxidising agent and amidoalcohol in the solvent. Although the ideal solvents are at least partially water miscible (e.g., tetrahydrofuran), the key is that, in the presence of oxidizing agent (e.g., aqueous sodium hypochlorite), at least two immiscible layers (e.g., a solvent-rich layer, normally the upper layer; and a water-rich layer, normally the lower layer) will form. Without wishing to be bound by theory, applicants believe it is important that the amidoalcohol not be in the same phase as the oxidizing agent when combined. Applicants have found that this can be accomplished in two different ways. According to claims a co-pending application, this can be done by partitioning the final product (amidocarboxylic acid) into a liquid organic solvent (i.e., using solvent that will form two phases, rather than forming one substantially aqueous phase). The exposed amide group on the alcohol comprising amide is thus protected from cleavage (e.g., through attack by the bleach which has partitioned mainly into separate liquid aqueous phase), and consequently far greater yield of carboxylic is produced. That is, it is important that, in the presence of the oxidizing agent, both a solvent rich layer (substantially free of oxidizing agent) and an aqueous layer (comprising substantially of the oxidizing agent) form. It should be noted that how quickly the two phase separation occurs is dependent generally on the scale of the reaction. Typically, the phase separation will occur in an hour or less, and can occur relatively instantaneously. A second way (as claimed in the subject invention) to maintain the oxidizing agent and the alcohol in separate phases, in this case in a liquid water phase and in a solid phase, is to use water alone as the solvent. The amidoalcohol is hydrophobic and does not dissolve or disperse into the agueous phase (it stays in solid phase), while the NaOCl remains in the continuous liquid aqueous phase. A reaction in which the solvent will form only one liquid phase (e.g., CH3CN/water solvent used in JP 10/087,554), thus, is not suitable and will form product in lower yield and purity. Surprisingly, solvents at opposite extremes of the polarity scale may be suitable for the reaction. Suitable polar solvents may include oxygenated hydrocarbons, more specifically cyclic and acyclic ethers and polyethers. Suitable non-polar solvents may include cyclic and acyclic aliphatic solvents, and aromatic solvents. Specific examples of cyclic oxygenated solvents (e.g. polar solvents) which may be used include tetrahydrofuren (THF) and dioxolane. Examples of acyclic oxygenated solvents include 1,2-dimethoxyethane, dimethoxymethane, diethoxymethane, and 2-methoxyethyl ether. It is preferred that the solvents do not contain anti¬oxidants (e.g., butylated hydroxyl toluene, abbreviated as BHT) as these anti-oxidants can interfere with the oxidation reaction. Such anti-oxidants are often found in cyclic and acyclic ethers and polyethers. Thus, preferably, solvents of the invention are substantially anti-oxidant free. Specific examples of cyclic aliphatic solvents (e.g., non-polar solvents) include cyclohexane; examples of acyclic aliphatic solvents include heptanes and hexanes; and examples of aromatic solvents include toluene, o, m, or p-xylene, and mixed xylenes. In preferred reaction, because of the consumption of oxidizing agent (e.g., sodium hypochlorite) and formation of carboxylic acid as consequence of the reaction, sufficient base should be used in the reaction to maintain pH above 6, more preferred above 7, preferably 8-9. An example of base which may be used is alkali metal hydroxide (e.g., NaOH). The base may be added to the oxidizing agent before the oxidizing agent is added to the reaction or, alternatively, the base may be added, for example, drop-wise during the course of the reaction as needed to maintain constant pH. The reaction itself typically takes place at room temperature, but is exothermic. Temperature rises of up to about 35°C occur without cooling. A cooling bath can be used to reduce the exotherm. A typical example of an oxidation of a monoethanolamide (N-lauroylmonoethanolamide, or MEA) to N-lauroylglycine (LG), as well as reaction conditions, isolation methology and rate of conversion to LG are set forth below: Reaction Conditions: Solvent: Tetrahydrofuran (THF)/Water Oxidizing agent: NaOCl (bleach, 11.5%, 3 eq.) + NaOH (base to maintain pH) Catalyst: KBr (co-catalyst), 4-Acetamido-TEMPO (abbreviated AA-TEMPO) Reaction temp: 25-30°C pH range: 12 (initial) to 6 (final) Reaction time: 1 - 4 hr. Isolation: THF extraction followed by solvent evaporation Typical conversion rate: 95 - 99% It should be noted that a mixture of N-lauroylglycine and sodium N-laurylglycinate (e.g., salt form) can be obtained depending on isolation pH and therefore, yields can be calculated separately for each. In the case where chlorine or chlorine containing molecule is used in the water solvent process, typically, after catalyst and oxidizing agent are added, reaction is given 30 minutes to 24 hours to run and the solution is then heated for 1 to 24 hours at a temperature of at least 40°C up to about 100°C. After heating, pH is acidified, and solid product is filtered from solution. EXAMPLES Protocol Extraction Technique to Isolate Carboxylic Acid (e.g., N-laurylglycine) At completion of oxidation reaction, reaction mixture is acidified to pH about 3.0 (e.g., by addition of HCl) and layers are separated. Lower aqueous layer is extracted with THF and the combined THF layers are concentrated on a rotary evaporator and dried in vacuo to give carboxylic acid (e.g., N-lauroylglycine) as a white solid. Extraction Technique to Isolate Alkali Metal or Alkaline Metal Salt of Carboxylic Acid (e.g.. Sodium N-Lauroylglycinate) The reaction here is the same as above except THF layer is separated without acidification. The aqueous layer must be in the range of 6-10, preferably 6-8. The aqueous layer is extracted {preferably twice) with THF. Combined THF layers are concentrated on a rotary evaporator and dried in vacuo to yield the salt (e.g., N-lauroylglycinate) Alternative Extraction Technique for the Carboxylic Acid Besides THF extraction, carboxylic acid can be isolated by a drowning procedure and filtration. In this procedure, the reaction mixture is acidified to pH about 2-3 and added to excess of water (about 3-4 volumes compared to reaction mixture volume) with vigorous stirring using a stirring paddle. Precipitate is collected by filtration, washed with water and dried in vacuo to give carboxylic acid (e.g., N-alkanoyl-glycine). Reaction Monitoring of Cocoyl MonoEthylAmide (CMEA) Oxidation to Cocoyl Glycinate (CG) by HPLC Instrument: Software: Column: Flow Rate: Sample: Injection Vol Mobile Phase: Gradient: Detection: Waters 2695 Separations Module equipped with a Waters 2996 Photodiode Array Detector Empower Pro (version 5.00, Waters Corp.) Restek Pinnacle DB C18 5um, 4.6 x 150mm maintained at 30 .C. 1 ml/min 1-2 mg/ml in 1:1 water:acetonitrile (W:ACN) containing 0.04% acetic acid (AcOH) 15 uL A = 2mM ammonium acetate, 0.04% AcOH B = 2mM ammonium acetate, 0.04% AcOH 90% aqueous ACN 95:5 A:B to 100% B (gradient, 35 min) followed by 100% B {isocratic, 5 min) 205nm Analysis of Sodium Cocoyl Glycinate Using Liquid Chromatography Mass Spectrometry (LC-MS) Instrument: Column: Flow Rate: Sample: water: Finnigan Mat LCQ; Restek Pinnacle DB C18 5um, 4.6 X 150 mm maintained at 30CC; 1 ml/min; l-2mg/ml for LC-MS and 50 ppm solution for infusion in 1:1 acetonitrile (W:Acn) containing 0.04% acetic acid (AcGR) and 2 mM ammonium acetate (AA); Mobile Phase: A = 2 mM ammonium acetate, 0.04% AcOH; B = 2 mM ammonium acetate, 0.04% AcOH, Acn:W (90:10) Gradient: Detection: 95:5 A:B to 100% B (gradient, 35 min) followed by 100% B (isocratic, 5 min); UV - 205 nm: MS - Electrospray Ionization (-) mode ; Analysis: For total ion count analysis, infusion was used as the sample injection method. A sample of cocoyl glycinate (acid form, 1 mg) is dissolved in THF (1 ml) and diluted by taking a 50 uL aliquot and diluting with 95 uL of THF. The diluted solution is directly infused into the mass spectrometer and the total ion count recorded. A representative total ion count spectrum of an infused cocoyl glycinate sample generated using the procedure described in Example 10 is shown in Figure 5 below. For LC-MS analysis, a 1 mg/ml glycinate sample prepared in mobile phase was separated by HPLC and analyzed by UV and MS. A representative total ion count spectrum of a reaction aliquot from oxidation of lauroyl monoethanolamide (C12 MEA) into lauroyl glycinate (C12 Glycinate) is shown in Figure 6 be1ow. Example 1. Oxidation of N~lauroylethanolamide {LMEA) in THF with 6.5 eg. of NaOCl, and Acid Work-up. 33 mg (4.5 mol%) of KBr (co-catalyst) was dissolved in 6 mL of water. Tetrahydrofuran solvent THF (31 mL) , AA-TEMPO catalyst (25 mg, 2.5 mol%) and 1.5 g N-lauroylethanolarnide (LMEA) were added with stirring to give a homogeneous water-white solution. Sodium hypochloride oxidizing agent (22 mL of 11.5% aq. Solution, 6.5 equivalents) and 2.3 mL of 2 NaOH (to maintain pH above 7) were mixed. The combined solution was added dropwise to the solution of LMEA and catalyst over a period of 1.5 hour. A separate aqueous layer immediately formed upon addition of the sodium hypochlorite solution. The pH of the aqueous layer was 12.7 after addition of the first 3.5 ml. The temperature was maintained below 32°C with an ice-water bath. The reaction was stirred for 0.5 hr. more until complete conversion of LMEA to LG as-determined by reversed-phase High Pressure Liquid Chromatography, abbreviated HPLC. The pH at end of the reaction was 7.6. At completion of the reaction, the mixture was acidified to pH 3.0 (to get the purified carboxylic acid) by addition of 8.5 mL of 1 N HC1, and the layers were separated. The lower aqueous layer was extracted with 30 mL THF, and the combined THF layers were concentrated on a rotary evaporator and dried in vacuo to give N-lauroylglycine in 116% yield (residual water present). Example 2. Oxidation of LMEA with 3.25 eg. of NaOCl, and Acid Work-up. The procedure in Example 1 was followed, except that the amount of sodium hypochlorite was decreased to 3.25 equivalents. The isolated yield was 103% (includes residual water), showing that the oxidation works with the lower sodium hypochlorite amount. Example 3. Oxidation of LMEA with 3.25 eg. of NaOCl, Isolation of Sodium Salt. In this example, sodium N-lauroylglycinate is obtained by a small modification of the isolation procedure. The procedure in Example 2 was followed. The pH was 7.8 upon completion of the reaction. In this case the THF layer was separated without acidification. The aq. layer was extracted twice with 30 mL of THF. After extraction, the pH of the aq. layer was 8.3. The combined THF layers were concentrated on a rotary evaporator and dried in vacuo to give sodium N-lauroylglycinate in 99% yield. Unlike N-lauroylglycine, the sodium N-lauroylglycinate dissolves in water and affords a foam upon agitation. Example 4. Oxidation of LMEA in THF with 6.5 eg. of NaOCl, Drowning Procedure at pH =2.6. The procedure of Example 1 was followed except for the isolation step. After completion of the reaction, the mixture was acidified to pH = 2.6 with 9.25 mL of 1 N HCl. The entire reaction mixture (both THF and water phases) were poured in 240 mL of water with vigorous stirring. The precipitated product was isolated by gravity filtration, and washed with 200 mL water. After air-drying, and further drying in vacuo, the product was obtained in 77% yield. The yield can be improved by better filtration techniques, e.g. by pressure filtration through a 0.45 Jim or less filter. Example 5. Oxidation of LMEA in THF with 3.25 eg. of N'aOCl, Drowning Procedure, Effect of pH on Yield. The procedure of Example 2 was followed except for the isolation step. After completion of the reaction, the mixture was only partially acidified (to pH = 5.2 with 3.6 mL of 1 N HCl.) The entire reaction mixture (both THF and water phases) were poured in 240 mL of water with vigorous stirring. The precipitated product was isolated by gravity filtration, and washed with 24 0 mL water. After drying in vacuo overnight, the product was obtained in 59% yield (based on free carboxylic acid), and 55% (based on the sodium carboxylate). The lower yield than Example 4 is attributed to the larger proportion of the water-soluble sodium carboxylate at the higher pH. Example 6. Oxidation of LMEA with 3.25 eg. of NaOCl in Water, Acid Work-up. KBr (33 mg, 4.5 mol%) and AA-TEMPO (25 mg, 2 mol%) were dissolved in 50 mL water. 1.50 g LMEA was added and the mixture stirred 1.5 hr. to form a homogeneous suspension. Dilute sodium hypochlorite (5%) was added in 2.0 mL increments over 1.3 hr. After each addition, 0.1 N HCl was added, if necessary to maintain a pH of 8-9. Details of the addition are given in the Table below: 5% NaOCl (mL) 0.1 N HCl pH 0.0 - 6.5 2.0 3.4 8.6 4.0 1.8 8.5 6.0 1.1 8.5 8.0 0.6 8.5 10.0 1.0 8.5 12.0 0.4 8.5 14.0 - 8.5 16.0 - 8.2 18.0 - 8.1 20.0 - 8.0 22.0 - 8.0 25.0 - 8.0 After stirring for 20.5 hr., the pH dropped to 5.9. The mixture was a translucent white emulsion. It was brought to 5 pH = 3.0 by addition of 3.5 mL of 1 N HCl, and extracted twice with 75 mL of THF. The combined THF layers were concentrated on a rotary evaporator and further dried in vacuo to give 1.81 g of N-lauroylglycine in 114% yield (includes residual water). Example 7. Oxidation of N-Cocoylmonoethanolamide (CMEA) with 3.25 eg. of NaOCl using Toluene as Solvent, Acid Work¬up. The oxidation reaction works on mixtures of monoethanolamides as well, including those derived from mixtures of fatty acids occurring in nature. In this example, N-cocoylmonoethanolamine (a mixture of C-8, C-10, C-12 (major component), C-14, C-16, and C-18 monoethanolamides) was oxidized under similar conditions to give a mixture of the corresponding N-cocoylglycines. KBr (33 mg, 4.5 mol%) and AA-TEMPO (25 mg, 2 mol%) were dissolved in 6 mL of water. CMEA (1.50 g, 6.16 mmol assuming 100% LG) was dissolved 60 mL toluene at 32°C, and the solution added to the KBr and AA-TEMPO. The stirred mixture was maintained at 31-37°C during the course of the addition and hold period. A solution of sodium hypochlorite (11 mL of 11.5% aq. solution, 3.25 eq.) and 1.15 mL of 2 N NaOH was added in 2.0 mL increments over a period of 50 min. The pH was 6.9 at the end of the addition. After 40 min. at 33°C, the pH was adjusted to 8.6 with 0.5 mL of 1 N NaOH. Stirring was continued for an additional 3.5 hr. and then the solution was allowed to cool to room temperature. The gelatinous reaction mixture was diluted with 70 mL THF and brought to pH = 2.2 with 5.5 mL of 1 N HCl. The layers were separated, and the aq. layer were extracted with an additional 20 mL THF. The combined THF layers were concentrated on a rotary evaporator and dried in vacuo to give of N-cocoylglycine in 84% yield. Example 8. Oxidation of N-Cocoylmonoethanolamide (CMEA) with 3.25 eq. of NaOCl using Cyclohexane as Solvent, Acid Work-up. The procedure of Example 4 was followed, except that the CMEA was dissolved in 120 mL cyclohexane at 43°C instead of toluene. After the reaction a translucent emulsion (pH = 6.2) was obtained. The emulsion was brought to pH 3.1 with 3.0 mL of 1 N HC1, and extracted twice with 100 mL THF. The combined THF layers were concentrated on a rotovap and dried in vacuo to give N-cocoylglycine in 73% yield. Comparative Example To show that correct solvent is required, applicants conducted an experiment comparing the reaction for production of N-lauroylmonoethanolamine as set forth in Example 5 in Japanese Patent Application 10/087,554 (Assigned to Lion Corp.) to the reaction of our invention. Results are set forth below. Process Parameter JP 10/087,554 Our Invention Cone, of Oxidant 5% (0.8 M) NaOCl 11.5% (1.85 M) NaOCl Amount of Oxidant 2.8 eq. NaOCl 3.25 eq. NaOCl Solvent Acetonitrile THF Phases Acetonitrile was dissolved in water and only one liquid phase formed 2-Phase System: Separate THF and aqueous layers. Two liquid phases were present Location of LMEA LMEA undissolved in CH3CN/water - thick slurry was obtained. LMEA dissolved in THF layer. Added base No NaOH added to NaOCl 2 N NaOH added to NaOCl pH Range pH 5.5 - 6.6 during reaction pH 13.2 - 7.4 during reaction Reaction Temperature 33-35°C 24-26°C Reaction Time 6 hr. including NaOCl addition time 2 hr. including NaOCl addition time. Isolated Yield 81% >100% (water present) Purity (HPLC Area%) 30.6% 68.5% 5 - 20 - Summary of Oxidation Examples A summary of the Examples for oxidation of LMEA to LG is set forth in the Table below. Ex. No NaOCl: Substrate NaOCl Cone. Solvent Reac Time (hr.) Initial Temp (°C) Peak Temp (°C) Initial pH Final pH Isolation Method Work¬up pH Yield as Acid Yield as Salt 1 6.5:1 11.5% THF 2 24 32 12.71 7.57 THF Extraction 3.0 116% 107% 2 3.25:1 11.5% THF 2 24 26 9.89 7.61 THF Extraction 2.1 103% 95% 3 3.25:1 11.5% THF 2 25.4 26.9 10.3 7.8 THF Extraction 8.3 108% 99% 4 6.5:1 11.5% THF 2 24.8 30.2 11.56 7.24 Water Drowning 2.6 77% 71% 5 3.25:1 11.5% THF 3 23 25.2 10.35 - Water Drowning 5.2 59% 55% 6 3.25 5% Water 21a 19.5 19.5 8.56 7.81 THF Extraction 2.5 114% 105% a) Actual reaction time may be less. A summary of the Examples of the oxidation of N-cocoylmethanolamide to N-cocoylglycine is set forth in the Table below. Ex. No NaOCl: Substrate NaOCl Cone. Solvent Reac Time (hr.) Initial Temp TO Peak Temp (°C) Initial pH Final pH Isolation Method Work¬up pH Yield as Acidb Yield as Saltb 7 3.25:1 11.5% Toluene 6 a 31 38 8.9 THF Extraction 2.2 84% 78% 8 3.25:1 11.5% Cyclo-hexane 16 a 38.5 41 6.2 THF Extraction 3.1 73% 67% 5 a) Actual reaction time may be less. b) Assume CMEA and CG are each the corresponding 100% C-12 compounds. Example 9. Oxidation of CMEA with 1.6 - 2.5 eq. of NaOCl in Water. CMEA (6g) was suspended in water (150mL) and stirred for 30 min at high speeds using a mechanical stirrer. AA-TEMPO {0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 1.6-2.5 eq.) under vigorous stirring maintaining the temperature between 22 to 33 °C. Between additions, the pH was maintained around 8 - 9 by adding IN NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 6 hours at 65 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N KCl and the white solid product filtered and dried under high vacuum 5.45g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 2 below. Example 10. Oxidation of CMEA with 2.3 - 3.2 eq. of NaOCl in Water. CMEA (6g) was suspended in water (150mL) and stirred for 3D min at high speeds using a mechanical stirrer. AA-TEMPO (0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 2.3-3.2 eq.) under vigorous stirring maintaining the temperature between 22 to 33 °C. Between additions, the pH was maintained around 8 - 9 by adding IN NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 8 hours at 60 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N HC1 and the white solid product filtered and dried under high vacuum 5.75g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 3 below. Example 11. Oxidation of CMEA with 3.2 - 4.0 eq. of NaOCl in Water. CMEA (6g) was suspended in water (150mL) and stirred for 30 min at high speeds using a mechanical stirrer. AA-TEMPO (0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 3.2-4 eq.) under vigorous stirring maintaining the temperature between 22 to 26 °C. Between additions, the pH was maintained around 8 - 9 by adding IN NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 8 hours at 60 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N HC1 and the white solid product filtered and dried under high vacuum 5.50g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 4 below. CLAIMS 1. A process for converting an alcohol comprising amide group to corresponding carboxylic acid in yield _>75% which process comprises reacting: R1 - CONR2 (CH2)mOH wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6, with an oxidizing agent in the presence of a hindered nitroxide radical and optional co-catalyst, wherein the solvent is solely water and, in the presence of the oxidizing agent, oxidizing agent separates into water, and the amidoalcohol stays or partitions in a solid organic layer to thereby permit the high yields noted. 2. A process according to claim 1, wherein the alcohol comprising amide group is an alkanoylmonoalkanolamine. 3. A process according to claim 2, wherein the alkanoylmonoalkanolamine is lauroyl monoalkanolamide or cocomonoethanolamide. 4. A process according to claim 1, wherein the oxidizing agent is selected from the group consisting of chlorine, a hypochlorite, chloroisocyanuric acid and mixtures thereof. 5. A process according to claim 1 wherein the oxidizing agent is selected from the group consisting of Na03r, bromosuccinimide, bromoisocyanuric acid, peracids, oxone, H2O2 and mixture thereof. 6. A process according to claim 1, wherein oxidizing agent is present in amount from equimolar to 8 molar. 7. A process according to claim 1, wherein the nitroxide catalyst is 4-acetamido-TEMPO. 8. A process according to claim 1, where, in addition to hindered nitroxide radical co-catalyst is used. 9. A process according to claim 8, wherein co-catalyst is alkali metal halide or alkali earth metal halide. 10. A process according to claim 1, wherein solvents contain substantially no anti-oxidants. 11. A process according to claim 1, where base is additionally added to the reaction. 12. A process according to claim 1, wherein sufficient base is added to maintain pH above 6. 13. A process according to claim 1, wherein the oxidizing agent is chlorine or chlorine containing molecule, wherein the oxidizing agent is added and reaction given 30 minutes to 24 hours to reach completion and wherein the resulting solution is heated for 1 to 24 hours at a temperature of at least 40°C to 100°C. Dated this 16th day of December 2008

Full Text

FORM - 2
THE PATENTS ACT, 1970
(39 of 1970)
&
The Patents Rules, 2003
COMPLETE SPECIFICATION
(See Section 10 and Rule 13)

PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS SOLVENT
HINDUSTAN UNILEVER LIMITED, a company incorporated under
the Indian Companies Act, 1913 and having its registered office
at 165/166, Backbay Reclamation, Mumbai -400 020, Maharashtra, India
The following specification particularly describes the invention and the manner in which it is to be performed

PROCESS FOR CONVERTING PRIMARY AMIDOALCOHOLS TO AMIDOCARBOXYLIC ACIDS IN HIGH YIELD USING WATER AS
SOLVENT
FIELD OF THE INVENTION
The present invention relates to a process for converting a compound or polymer comprising a primary alcohol and an amide group to amidocarboxylic acid. In particular, the primary amido alcohol is converted to carboxylic acid in unexpectedly high yields when proper solvent (e.g., water) is selected. In addition, when chlorine or chlorinated molecules are used as oxidizing agents, specific processing parameters used in one embodiment of the invention ensure that chlorinated amido nitrogen is not formed.
BACKGROUND
Amidocarboxylic acids are desirable surfactants in that they have good water solubility, good detergency and foaming properties and are mild to skin and hair. One method for the production of such surfactant is through the oxidation of an alcohol containing an amide group (e.g., coco mono-ethanolamide or CMEA).
The problem, however, is that it is very difficult to drive the oxidation of alcohol to carboxylic acid efficiently. The reaction will often stop at the aldehyde stage, and the yields of carboxylic acid as final products are qvite low.

Japanese Patent Laid-open No. 05/194,334 (Sandoz) discloses a process in which a hydroxyl containing compound (which may be, for example, alkyl amide polyoxyalkanol) is made to react with at least an equimolar amount of inorganic or organic halogen-containing oxidizing agent, e.g. NaOCl, in the presence of weak base and a catalytic amount of hindered nitroxide as exemplified by 2, 2, 6, 6-
tetramethylpiperidine 1-oxyl, hereafter abbreviated TEMPO, and chemical derivatives thereof. In this patent, no yield or purity information is given. The process disclosed is limited to alcohols which have polyethylene glycol or polypropylene glycol substitution, or to polyglucosides, as starting reactants. Such compounds are water-soluble or water-dispersible, which makes possible the use of water as the solvent. The patent does not teach a process using hydrophobic primary alcohols (i.e., amido alcohols) of the invention as starting reactant.
Japanese Patent Laid Open No. 04/283,537 (Shell) discloses a process using an oxidizing agent such as sodium hypochlorite in the presence of TEMPO. The process relates to production of an alkoxyalkanoic acid from the corresponding alkoxyalkanol, however, and not to the production of an amidecarboxylic acid from an alcohol having an amide group.
Japanese Laid Open No. 10/087,554 (Lion Corporation) discloses a process for production of amidocarboxylic acid from alcohol having an amide group using an oxidizing agent of chlorine type (e.g. NaOCl) in the presence of a nitroxide radical (e.g., TEMPO) and further in the presence of alkali metal halide or alkali earth metal halide (e.g., potassium

chloride). In Examples 3 and 5, for example, an alcohol comprising amide; a nitroxide radical; and a 10% solution of alkali metal chloride (potassium or sodium bromide) in water, additional water, and acetonitrile (solvent) are charged into a beaker and stirred. Under these conditions, the acetonitrile and water mix together to form a single liquid phase. In each example, the purity of the carboxylic acid is calculated from the acid value, but nothing is stated about yield. The acid value is not selective for the desired carboxylic acid, but would include all acid components present.
Unexpectedly, applicants have now found that the type of solvent or solvents used during the oxidation reaction is critical to the yield of product (carboxylic acid). Without wishing to be bound by theory, applicants believe the starting amidoalcohol must not be in the same phase as the oxidizing agent. Applicants have found that this separation of oxidizing agent and alcohol can be accomplished in at least two different ways. According to a separate application applicants have filed on same date as the subject application, the final product (e.g.,
amidocarboxylic acid) is partitioned into an organic solvent (i.e., using solvent that will form both a hydrophobic liquid phase and an aqueous liquid phase, rather than forming one substantially aqueous phase). In this manner, the exposed amide group on the amidoalcohol is protected from cleavage (e.g., the bleach which has partitioned mainly into aqueous phase will not attack the amidoalcohol in the separate phase), and consequently far greater yield of amidocarboxylic acid is produced. That is, it is important

that, in the presence of the oxidizing agent, both a solvent rich layer (substantially free of oxidising agent) and an aqueous layer {comprising substantially of the oxidizing agent) form.
In a second embodiment, which is claimed in the subject application, the oxidizing agent and the alcohol are also maintained in separate phases. Here, however, the two phases are a water phase and a solid phase, and water alone is used as the solvent. That is, the amidoalcohol, which is hydrophobic, does not dissolve or disperse into the aqueous phase (rather it stays in the solid, non-aqueous phase) while the NaOCl remains in the continuous aqueous phase. In a preferred aspect of this embodiment (water as solvent), when chlorine or chlorinated molecule (e.g., NaOCl) is used as oxidizing agent, specific process steps (i.e., heating) must be used to ensure the amido nitrogen of the final carboxylic acid is not chlorinated as this would be an undesirable by-product.
As indicated, the subject application relates to processes where water is employed as solvent and, upon addition of oxidizing agent, the oxidizing agent partitions into solvent while amidoalcohol and/or amidocarboxylic acid stay in solid phase.
BRIEF DESCRIPTION OF THE INVENTION
The present invention provides a process for converting primary alcohol having an amide group to amidocarboxylic acid in high yield (e.g., >75, preferably >80%, more

preferably >85%, more preferably ≥90% yield) which process comprises reacting a primary alcohol having amide group (amidoalcohol) with an oxidizing agent, preferably a chlorine-containing oxidant like NaOCl, in the presence of a nitroxide radical and optionally in the presence of an alkali metal halide or alkali earth metal halide. In this process the solvent in which the reaction takes place is selected such that, in the presence of the oxidizing agent, the primary amidoalcohol partitions or stays (after addition of bleach or other oxidizing agent) in the solid organic phase, while bleach or oxidizing agent partitions substantially into liquid aqueous phase. Such partitioning ensures the high yields noted above (e.g., the amide linkage is not available to be cleaved by the oxidizing agent because the oxidizing agent has partitioned into liquid aqueous phase). In other words, the amidoalcohol stays in a solid phase and oxidizing agent partitions quickly enough into the agueous phase to avoid formation of undesired by¬product. It is completely unexpected that using water as sole solvent chosen could make such critical difference.
It is also a critical aspect of the invention that the catalyst used in this reaction be a hindered nitroxide radical. An optional alkali metal halide or alkali earth metal halide co-catalyst may also to be used, or the co-catalyst can be, for example, sodium tetraborate.
Specifically, in one embodiment of the invention, sufficient base (e.g., sodium hydroxide) is added to the reaction to ensure reaction takes place at a pH above 6, preferably 7 to 10, more preferably 7.5 to 9, even more preferably 8 to 9.

Addition of base is used to make up for consumption of oxidizing agent (e.g., sodium hypochlorite) during formation of amidocarboxylic acid. Base may be added to the oxidizing agent solution prior to addition of the oxidizing agent to the reaction or it may be added during the course of the reaction {e.g., to maintain constant pH).
These and other aspects, features and advantages will become apparent to those of ordinary skill in the art from a reading of the following detailed description and the appended claims. For the avoidance of doubt, any feature of one aspect of the present invention may be utilized in any other aspect of the invention. It is noted that the examples given in the description below are intended to clarify the invention and are not intended to limit the invention to those examples per se. Other than in the experimental examples, or where otherwise indicated, all numbers expressing quantities of ingredients or reaction conditions used herein are to be understood as modified in all instances by the term "about". Similarly, all percentages are weight/weight percentages of the total composition unless otherwise indicated. Numerical ranges expressed in the format "from x to y" are understood to include x and y. When for a specific feature multiple preferred ranges are described in the format "from x to y", it is understood that all ranges combining the different endpoints are also contemplated. Where the term "comprising" is used in the specification or claims, it is not intended to exclude any terms, steps or features not specifically recited. All temperatures are in degrees Celsius (°C) unless specified otherwise. All measurements

are in SI units unless specified otherwise. All documents cited are - in relevant part - incorporated herein by reference.
BRIEF DESCRIPTION OF THE DRAWING
Figure 1 is a liquid chromatogram (HPLC-UV-Vis) profile of products formed when reaction was carried out in CH3CN/water solvent and only a single liquid phase was formed (bottom figure, corresponding to example of JP 10/087,554 reference to Lion), compared to when solvent was THF/water and formed two liquid phases (top). In Figures 1-4, AU refers to Absorbance Units.
As observed, a solvent which partitions into two liquid phases leads to high yields of N-lauroylglycine (LG) from N-lauroylmonoethanolamide (LMEA) starting material. By contrast, when the organic solvent formed a single liquid phase with the water, the yield and purity of LG (glycinate) were lower. Thus, for example, the pure LG product was predominantly formed at 13.54 minutes when two liquid phases formed but, when only one phase formed, there were huge amounts of impurities at 15.80 seconds.
Figure 2 is a graph of an HPLC-UV-Vis analysis of cocoyl monoethanolamide (CMEA) oxidation to the carboxylic acid using 1.6 to 2.5 equivalents of NaOCl. Top panel is CMEA reagent before addition of NaOCl; Middle panel B is analysis of product using water process two hours after addition of NaOCl and before heating; and bottom panel C is analysis of product using the water process 24 hours after

addition of NaOCl and with further heating at 80°C for 4 hours. As seen, when no heating step is used (Panel B) a C12 N-Cl glycinate intermediate is formed (i.e., between minute 22 and 23) while such chlorinated intermediate is not formed when heating step is used.
Figure 3 is graph similar to Figure 2 but using 2.3 to 3.2 equivalents NaOCl to oxidize CMEA to cocoyl glycinate. Panels A again shows CMEA before addition of NaOCl, Panel B is reaction mixture 1 hour after NaOCl addition and Panel C is reaction24 hours after addition of NaOCl and further heating at 65° for 6 hours. Again, it is seen that, without heating step, C12 N-Cl glycinate intermediate is formed and such intermediate is not formed when heating step is used.
Figure 4 is reaction profile of CMEA oxidation to cocoyl glycinate using 3.2 to 4.0 eq. of NaOCl. Panel A is CMEA before addition of NaOCl, Panel B is reaction 24 hours after addition of NaOCl and Panel C is mixture 24 hours after addition of NOCl and further heating at 60°C for 8 hours. Again, in absence of heating step, C12 N-Cl glycinate will form.
Figure 5 is a representative total ion count spectrum of an infused cocoyl glycinate sample generated using the procedure described in Example 10. This spectrum demonstrates the absence of cocoyl N-Cl glycinate intermediate.
For LC-MC analysis, a 1 mg/ml glycinate sample prepared in mobile phase was separated by HPLC and analyzed by UV and

MS. A representative HPLC chromatogram with total ion count mass detection profile of a reaction aliquot from oxidation of lauroyl monoethanalamide (C12 MEA) into lauryl glycinate (C12 glycinate) is shown in Figure 6.
DETAILED DESCRIPITON OF THE INVENTION
The present invention relates to a novel and improved process for converting a primary alcohol comprising an amide group (e.g., C8-C22 alkoylmonoalkanolamide such as lauroyl monoethanolamide) to the corresponding amidocarboxylic acid (e.g., mixture of N-lauroyl glycine and alkalimetal N-lauroyl glycinate), and which process provides very high yields of product (e.g., ≥75%, preferably ≥ 80%, more preferably ^ 85% yield). More specifically the process comprises reacting a primary alcohol comprising such amide group with an oxidizing agent in the presence of a nitroxide radical and optional catalyst {e.g., alkali metal halide), wherein the solvent in which the reaction takes place is selected in such way that two phases separating the amidoalcohol from the oxidizing agent are formed. In other words, the amidoalcohol stays or is partitioned into an organic phase of the two phase system thereby and the oxidizing agent stays predominantly in the aqueous phase. This protects the amide group on the amidoalcohol from further cleavage and provides the high yields as noted. In the specific embodiment of the claimed invention, the amidoalcohol is separated from the oxidizing agent using only water as solvent in that the oxidizing agent partitions into the liquid aqueous water phase while the amidoalcohol stays in the undissolved solid state (heterogeneous solid-

liquid system). In a preferred embodiment of this water solvent process, after addition of oxidizing agent (e.g., NaOCl), the reaction is allowed to run to completion. This generally takes 30 minutes to 24 hours, typically 1 to 10 hours. The reaction is then heated to a temperature of at least 40 up to 100°C for between 1 to 24 hours. The heating step is not necessary if non chlorine containing molecule is used in the water process because, in such case, chlorinated amido nitrogen does not form.
More specifically, the starting reactant of the subject invention is an alcohol having an amide group which may be defined as follows:
R2-CONR2 (CH2)m OH
wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6.
Examples of compounds which may be encompassed by the structure are N-alkanoylmonoethanolamines such as N-lauroylmonoethanolamide (LMEA) or N-cocoylmonoethanolamide (CMEA).
The starting product may be a mixture of monoalkanolamides (e.g., monoethanolamine) including those derived from mixtures of fatty acids found in nature. N-cocoyl monoethanolamine, for example may comprise a mixture of Ca,

C10 and C12 fatty acids as major component mixed with c14, C16 and C18 fatty acids.
The oxidizing agent used to oxidize the starting alcohol can be any oxidizing agent which will allow the alcohol group to be oxidized to carboxylic acid. Typically, such oxidizing agents include those of the chlorine type. These may include chlorine, a hypochlorite (e.g., alkali metal hypochlorite), trichloroisocyanuric acid and dichloroisocyononic acid. Preferred oxidizing agents include sodium hypochlorite (e.g., industrial grade bleach comprises 5% to 13% sodium hypochlorite), calcium hypochlorite, chlorine itself, and organic chlorine-containing compounds, for example trichloroisocyanuric acid. Non-chlorine containing oxidants may be used, for example, oxone (2KHS05'KHS04'K2S04) , NaOBr, N-bromosuccinimide, or tribromoisocyanuric acid. Non-halogen containing antioxidants may also be used, as exemplified by H2O2, optionally in the presence of sodium tungstate dihydrate catalyst.
The amount of oxidizing agent may vary, but typically eguimolar to 8 molar, preferably 1 to 7 equivalents, more preferably 2 to 6 molar are used.
The starting alcohol of the invention is oxidized with an oxidizing agent (as noted above) in the presence of a hindered piperidinyloxy radical catalyst (nitroxide) and optionally in the presence of co-catalyst as are described below.

The nitroxide catalyst radical used in the invention (e.g., hindered nitroxide) is produced by oxidation of a cyclic or acyclic secondary amine containing no a-hydrogens (i.e., there are no hydrogens on the carbon adjacent to N) with peroxide, or by oxidation of the corresponding hydroxylamine. Examples of stable nitroxide radicals suitable for use in this invention are mentioned in the following documents. These include linear, cyclic, dicyclic or macromolecular compounds to which one or more nitroxyl radicals are connected.
Chem. Review, 78, 37 (1979):
G. Rozantsev, "Free Nitroxyl Radicals", Penum Publishing Corporation, New York, 1970; and E. G. Rozantsev, V. D., Scholle, Synthesis, 1971,190. Preferred examples of the nitroxide radical are as follows.
2,2,6,6-Tetramethyl-piperidine 1-oxyl (TEMPO); 2,2,5,5-Tetramethyl-pyrrolidine 1-oxyl; and l-Aza-2,2,7,7-tetramethyl-cycloheptane 1-oxyl.
TEMPO and chemical derivatives thereof are preferred, examples of which follow:
4-Hydroxyl-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Methoxy-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Ethoxy-2-2,6,6-tetramethyl-piperidine 1-oxyl; 4-Acetylamido-2-2,6,6-tetramethyl-piperidine 1-oxyl; 4-Carbamoyl-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Benzoylamino-2,2,6,6-tetramethyl-piperidine 1-oxyl; 4-Oxo-2,2, 6, 6-tetramethyl-piperidine 1-oxyl;

2,2, 6, 6-Tetramethyl-piperidine-l-oxyl 4-sulfate;
2,2,6,6-Tetramethyl-piperidine-l-oxyl 4-phosphate; and
3-Carbamoyl-2,2,6,6-tetramethyl-pyrrolidine 1-oxyl.
UV light stabilizers containing 2,2,6,6-
tetramethylpiperidine functionality (Hindered Amine Light Stabilizers, abbreviated HALS), both monomeric and oligomeric, can serve as precursors to stable nitroxyl radicals by oxidation as well.
It is also possible that an amine or a hydroxylamine which is a precursor thereof is used and, in the actual case, it is oxidized and then used. The amount of the nitroxide radical used to 1 equivalent of the starting alcohol material is typically from 0.01 to 10 mol% or, preferably, from 0.1 to 5 mol% based on amidoalcohol.
An optional co-catalyst is often used with the nitroxide radical primary catalyst. The co-catalyst, if used, may be for example an alkali metal halide or alkali earth metal halide. These may include alkali metal bromide, e.g. sodium bromide, and alkali metal chloride, e.g. sodium chloride, and potassium chloride, alkali earth metal bromide, e.g. calcium bromide and magnesium bromide, alkali earth metal chloride, e.g. calcium chloride, and magnesium chloride.
Typically the co-catalyst is used from 0.01 to 10 mole%, preferably 0.1 to 5 mol% equivalent based on amidoalcohol. Sodium tetraborate may be used in place of the bromide or chloride.

Solvent
The key to the invention resides in the selection of proper solvent, i.e., solvent which will partition into organic phase and aqueous phase upon combination of oxidising agent and amidoalcohol in the solvent.
Although the ideal solvents are at least partially water miscible (e.g., tetrahydrofuran), the key is that, in the presence of oxidizing agent (e.g., aqueous sodium hypochlorite), at least two immiscible layers (e.g., a solvent-rich layer, normally the upper layer; and a water-rich layer, normally the lower layer) will form.
Without wishing to be bound by theory, applicants believe it is important that the amidoalcohol not be in the same phase as the oxidizing agent when combined. Applicants have found that this can be accomplished in two different ways. According to claims a co-pending application, this can be done by partitioning the final product (amidocarboxylic acid) into a liquid organic solvent (i.e., using solvent that will form two phases, rather than forming one substantially aqueous phase). The exposed amide group on the alcohol comprising amide is thus protected from cleavage (e.g., through attack by the bleach which has partitioned mainly into separate liquid aqueous phase), and consequently far greater yield of carboxylic is produced. That is, it is important that, in the presence of the oxidizing agent, both a solvent rich layer (substantially free of oxidizing agent) and an aqueous layer (comprising substantially of the oxidizing agent) form. It should be noted that how quickly

the two phase separation occurs is dependent generally on the scale of the reaction. Typically, the phase separation will occur in an hour or less, and can occur relatively instantaneously.
A second way (as claimed in the subject invention) to maintain the oxidizing agent and the alcohol in separate phases, in this case in a liquid water phase and in a solid phase, is to use water alone as the solvent. The amidoalcohol is hydrophobic and does not dissolve or disperse into the agueous phase (it stays in solid phase), while the NaOCl remains in the continuous liquid aqueous phase.
A reaction in which the solvent will form only one liquid phase (e.g., CH3CN/water solvent used in JP 10/087,554), thus, is not suitable and will form product in lower yield and purity.
Surprisingly, solvents at opposite extremes of the polarity scale may be suitable for the reaction. Suitable polar solvents may include oxygenated hydrocarbons, more specifically cyclic and acyclic ethers and polyethers. Suitable non-polar solvents may include cyclic and acyclic aliphatic solvents, and aromatic solvents.
Specific examples of cyclic oxygenated solvents (e.g. polar solvents) which may be used include tetrahydrofuren (THF) and dioxolane. Examples of acyclic oxygenated solvents include 1,2-dimethoxyethane, dimethoxymethane, diethoxymethane, and 2-methoxyethyl ether.

It is preferred that the solvents do not contain anti¬oxidants (e.g., butylated hydroxyl toluene, abbreviated as BHT) as these anti-oxidants can interfere with the oxidation reaction. Such anti-oxidants are often found in cyclic and acyclic ethers and polyethers. Thus, preferably, solvents of the invention are substantially anti-oxidant free.
Specific examples of cyclic aliphatic solvents (e.g., non-polar solvents) include cyclohexane; examples of acyclic aliphatic solvents include heptanes and hexanes; and examples of aromatic solvents include toluene, o, m, or p-xylene, and mixed xylenes.
In preferred reaction, because of the consumption of oxidizing agent (e.g., sodium hypochlorite) and formation of carboxylic acid as consequence of the reaction, sufficient base should be used in the reaction to maintain pH above 6, more preferred above 7, preferably 8-9. An example of base which may be used is alkali metal hydroxide (e.g., NaOH).
The base may be added to the oxidizing agent before the oxidizing agent is
added to the reaction or, alternatively, the base may be added, for example, drop-wise during the course of the reaction as needed to maintain constant pH.
The reaction itself typically takes place at room temperature, but is exothermic. Temperature rises of up to about 35°C occur without cooling. A cooling bath can be used to reduce the exotherm.

A typical example of an oxidation of a monoethanolamide (N-lauroylmonoethanolamide, or MEA) to N-lauroylglycine (LG), as well as reaction conditions, isolation methology and rate of conversion to LG are set forth below:

Reaction Conditions:
Solvent: Tetrahydrofuran (THF)/Water
Oxidizing agent: NaOCl (bleach, 11.5%, 3 eq.)
+ NaOH (base to maintain pH) Catalyst: KBr (co-catalyst), 4-Acetamido-TEMPO
(abbreviated AA-TEMPO) Reaction temp: 25-30°C
pH range: 12 (initial) to 6 (final) Reaction time: 1 - 4 hr. Isolation: THF extraction followed by solvent
evaporation Typical conversion rate: 95 - 99%
It should be noted that a mixture of N-lauroylglycine and sodium N-laurylglycinate (e.g., salt form) can be obtained depending on isolation pH and therefore, yields can be calculated separately for each.
In the case where chlorine or chlorine containing molecule is used in the water solvent process, typically, after catalyst and oxidizing agent are added, reaction is given 30

minutes to 24 hours to run and the solution is then heated
for 1 to 24 hours at a temperature of at least 40°C up to
about 100°C. After heating, pH is acidified, and solid
product is filtered from solution.
EXAMPLES
Protocol
Extraction Technique to Isolate Carboxylic Acid (e.g., N-laurylglycine)
At completion of oxidation reaction, reaction mixture is acidified to pH about 3.0 (e.g., by addition of HCl) and layers are separated. Lower aqueous layer is extracted with THF and the combined THF layers are concentrated on a rotary evaporator and dried in vacuo to give carboxylic acid (e.g., N-lauroylglycine) as a white solid.
Extraction Technique to Isolate Alkali Metal or Alkaline Metal Salt of Carboxylic Acid (e.g.. Sodium N-Lauroylglycinate)
The reaction here is the same as above except THF layer is separated without acidification. The aqueous layer must be in the range of 6-10, preferably 6-8. The aqueous layer is extracted {preferably twice) with THF. Combined THF layers are concentrated on a rotary evaporator and dried in vacuo to yield the salt (e.g., N-lauroylglycinate)

Alternative Extraction Technique for the Carboxylic Acid
Besides THF extraction, carboxylic acid can be isolated by a drowning procedure and filtration. In this procedure, the reaction mixture is acidified to pH about 2-3 and added to excess of water (about 3-4 volumes compared to reaction mixture volume) with vigorous stirring using a stirring paddle. Precipitate is collected by filtration, washed with water and dried in vacuo to give carboxylic acid (e.g., N-alkanoyl-glycine).
Reaction Monitoring of Cocoyl MonoEthylAmide (CMEA) Oxidation to Cocoyl Glycinate (CG) by HPLC

Instrument:
Software: Column:
Flow Rate: Sample:
Injection Vol Mobile Phase:
Gradient:
Detection:

Waters 2695 Separations Module equipped with
a Waters 2996 Photodiode Array Detector
Empower Pro (version 5.00, Waters Corp.)
Restek Pinnacle DB C18 5um, 4.6 x 150mm
maintained at 30 .C.
1 ml/min
1-2 mg/ml in 1:1 water:acetonitrile (W:ACN)
containing 0.04% acetic acid (AcOH)
15 uL
A = 2mM ammonium acetate, 0.04% AcOH
B = 2mM ammonium acetate, 0.04% AcOH 90%
aqueous ACN
95:5 A:B to 100% B (gradient, 35 min)
followed by 100% B {isocratic, 5 min)
205nm

Analysis of Sodium Cocoyl Glycinate Using Liquid
Chromatography Mass Spectrometry (LC-MS)

Instrument: Column:
Flow Rate: Sample:
water:
Finnigan Mat LCQ;
Restek Pinnacle DB C18 5um, 4.6 X 150 mm maintained at 30CC; 1 ml/min;
l-2mg/ml for LC-MS and 50 ppm solution for infusion in 1:1
acetonitrile (W:Acn) containing 0.04% acetic acid (AcGR)
and 2 mM ammonium acetate (AA); Mobile Phase: A = 2 mM ammonium acetate, 0.04% AcOH;
B = 2 mM ammonium acetate, 0.04% AcOH, Acn:W (90:10)
Gradient:
Detection:
95:5 A:B to 100% B (gradient, 35 min) followed by 100% B (isocratic, 5 min);
UV - 205 nm: MS - Electrospray Ionization (-) mode ;
Analysis: For total ion count analysis, infusion was used as the sample injection method. A sample of cocoyl glycinate (acid form, 1 mg) is dissolved in THF (1 ml) and diluted by taking a 50 uL aliquot and diluting with 95 uL of THF. The diluted solution is directly infused into the mass spectrometer and the total ion count recorded. A representative total ion count spectrum of an infused cocoyl glycinate sample generated using the procedure described in Example 10 is shown in Figure 5 below. For LC-MS analysis, a 1 mg/ml glycinate sample prepared in mobile phase was

separated by HPLC and analyzed by UV and MS. A representative total ion count spectrum of a reaction aliquot from oxidation of lauroyl monoethanolamide (C12 MEA) into lauroyl glycinate (C12 Glycinate) is shown in Figure 6 be1ow.
Example 1. Oxidation of N~lauroylethanolamide {LMEA) in THF with 6.5 eg. of NaOCl, and Acid Work-up. 33 mg (4.5 mol%) of KBr (co-catalyst) was dissolved in 6 mL of water. Tetrahydrofuran solvent THF (31 mL) , AA-TEMPO catalyst (25 mg, 2.5 mol%) and 1.5 g N-lauroylethanolarnide (LMEA) were added with stirring to give a homogeneous water-white solution. Sodium hypochloride oxidizing agent (22 mL of 11.5% aq. Solution, 6.5 equivalents) and 2.3 mL of 2 NaOH (to maintain pH above 7) were mixed. The combined solution was added dropwise to the solution of LMEA and catalyst over a period of 1.5 hour. A separate aqueous layer immediately formed upon addition of the sodium hypochlorite solution. The pH of the aqueous layer was 12.7 after addition of the first 3.5 ml. The temperature was maintained below 32°C with an ice-water bath. The reaction was stirred for 0.5 hr. more until complete conversion of LMEA to LG as-determined by reversed-phase High Pressure Liquid Chromatography, abbreviated HPLC. The pH at end of the reaction was 7.6.
At completion of the reaction, the mixture was acidified to pH 3.0 (to get the purified carboxylic acid) by addition of 8.5 mL of 1 N HC1, and the layers were separated. The lower aqueous layer was extracted with 30 mL THF, and the combined THF layers were concentrated on a rotary evaporator and

dried in vacuo to give N-lauroylglycine in 116% yield (residual water present).
Example 2. Oxidation of LMEA with 3.25 eg. of NaOCl, and Acid Work-up. The procedure in Example 1 was followed, except that the amount of sodium hypochlorite was decreased to 3.25 equivalents. The isolated yield was 103% (includes residual water), showing that the oxidation works with the lower sodium hypochlorite amount.
Example 3. Oxidation of LMEA with 3.25 eg. of NaOCl, Isolation of Sodium Salt. In this example, sodium N-lauroylglycinate is obtained by a small modification of the isolation procedure. The procedure in Example 2 was followed. The pH was 7.8 upon completion of the reaction. In this case the THF layer was separated without acidification. The aq. layer was extracted twice with 30 mL of THF. After extraction, the pH of the aq. layer was 8.3. The combined THF layers were concentrated on a rotary evaporator and dried in vacuo to give sodium N-lauroylglycinate in 99% yield. Unlike N-lauroylglycine, the sodium N-lauroylglycinate dissolves in water and affords a foam upon agitation.
Example 4. Oxidation of LMEA in THF with 6.5 eg. of NaOCl, Drowning Procedure at pH =2.6. The procedure of Example 1 was followed except for the isolation step. After completion of the reaction, the mixture was acidified to pH = 2.6 with 9.25 mL of 1 N HCl. The entire reaction mixture (both THF and water phases) were poured in 240 mL of water with vigorous stirring. The precipitated product was

isolated by gravity filtration, and washed with 200 mL water. After air-drying, and further drying in vacuo, the product was obtained in 77% yield. The yield can be improved by better filtration techniques, e.g. by pressure filtration through a 0.45 Jim or less filter.
Example 5. Oxidation of LMEA in THF with 3.25 eg. of N'aOCl, Drowning Procedure, Effect of pH on Yield. The procedure of Example 2 was followed except for the isolation step. After completion of the reaction, the mixture was only partially acidified (to pH = 5.2 with 3.6 mL of 1 N HCl.) The entire reaction mixture (both THF and water phases) were poured in 240 mL of water with vigorous stirring. The precipitated product was isolated by gravity filtration, and washed with 24 0 mL water. After drying in vacuo overnight, the product was obtained in 59% yield (based on free carboxylic acid), and 55% (based on the sodium carboxylate). The lower yield than Example 4 is attributed to the larger proportion of the water-soluble sodium carboxylate at the higher pH.
Example 6. Oxidation of LMEA with 3.25 eg. of NaOCl in Water, Acid Work-up. KBr (33 mg, 4.5 mol%) and AA-TEMPO (25 mg, 2 mol%) were dissolved in 50 mL water. 1.50 g LMEA was added and the mixture stirred 1.5 hr. to form a homogeneous suspension. Dilute sodium hypochlorite (5%) was added in 2.0 mL increments over 1.3 hr. After each addition, 0.1 N HCl was added, if necessary to maintain a pH of 8-9.
Details of the addition are given in the Table below:

5% NaOCl (mL) 0.1 N HCl pH
0.0 - 6.5
2.0 3.4 8.6
4.0 1.8 8.5
6.0 1.1 8.5
8.0 0.6 8.5
10.0 1.0 8.5
12.0 0.4 8.5
14.0 - 8.5
16.0 - 8.2
18.0 - 8.1
20.0 - 8.0
22.0 - 8.0
25.0 - 8.0
After stirring for 20.5 hr., the pH dropped to 5.9. The mixture was a translucent white emulsion. It was brought to 5 pH = 3.0 by addition of 3.5 mL of 1 N HCl, and extracted twice with 75 mL of THF. The combined THF layers were concentrated on a rotary evaporator and further dried in vacuo to give 1.81 g of N-lauroylglycine in 114% yield (includes residual water).

Example 7. Oxidation of N-Cocoylmonoethanolamide (CMEA) with 3.25 eg. of NaOCl using Toluene as Solvent, Acid Work¬up. The oxidation reaction works on mixtures of monoethanolamides as well, including those derived from mixtures of fatty acids occurring in nature. In this example, N-cocoylmonoethanolamine (a mixture of C-8, C-10, C-12 (major component), C-14, C-16, and C-18 monoethanolamides) was oxidized under similar conditions to give a mixture of the corresponding N-cocoylglycines. KBr (33 mg, 4.5 mol%) and AA-TEMPO (25 mg, 2 mol%) were dissolved in 6 mL of water. CMEA (1.50 g, 6.16 mmol assuming 100% LG) was dissolved 60 mL toluene at 32°C, and the solution added to the KBr and AA-TEMPO. The stirred mixture was maintained at 31-37°C during the course of the addition and hold period. A solution of sodium hypochlorite (11 mL of 11.5% aq. solution, 3.25 eq.) and 1.15 mL of 2 N NaOH was added in 2.0 mL increments over a period of 50 min. The pH was 6.9 at the end of the addition. After 40 min. at
33°C, the pH was adjusted to 8.6 with 0.5 mL of 1 N NaOH. Stirring was continued for an additional 3.5 hr. and then the solution was allowed to cool to room temperature.
The gelatinous reaction mixture was diluted with 70 mL THF and brought to pH = 2.2 with 5.5 mL of 1 N HCl. The layers were separated, and the aq. layer were extracted with an additional 20 mL THF. The combined THF layers were concentrated on a rotary evaporator and dried in vacuo to give of N-cocoylglycine in 84% yield.
Example 8. Oxidation of N-Cocoylmonoethanolamide (CMEA) with 3.25 eq. of NaOCl using Cyclohexane as Solvent, Acid

Work-up. The procedure of Example 4 was followed, except that the CMEA was dissolved in 120 mL cyclohexane at 43°C instead of toluene. After the reaction a translucent emulsion (pH = 6.2) was obtained. The emulsion was brought to pH 3.1 with 3.0 mL of 1 N HC1, and extracted twice with 100 mL THF. The combined THF layers were concentrated on a rotovap and dried in vacuo to give N-cocoylglycine in 73% yield.
Comparative Example
To show that correct solvent is required, applicants conducted an experiment comparing the reaction for production of N-lauroylmonoethanolamine as set forth in Example 5 in Japanese Patent Application 10/087,554 (Assigned to Lion Corp.) to the reaction of our invention. Results are set forth below.

Process Parameter JP 10/087,554 Our Invention

Cone, of Oxidant 5% (0.8 M) NaOCl 11.5% (1.85 M) NaOCl
Amount of Oxidant 2.8 eq. NaOCl 3.25 eq. NaOCl
Solvent Acetonitrile THF
Phases Acetonitrile was dissolved in water and only one liquid phase formed 2-Phase System: Separate THF and aqueous layers. Two liquid phases were present
Location of LMEA LMEA undissolved in CH3CN/water - thick slurry was obtained. LMEA dissolved in THF layer.
Added base No NaOH added to NaOCl 2 N NaOH added to NaOCl
pH Range pH 5.5 - 6.6 during reaction pH 13.2 - 7.4 during reaction
Reaction Temperature 33-35°C 24-26°C
Reaction Time 6 hr. including NaOCl addition time 2 hr. including NaOCl addition time.
Isolated Yield 81% >100% (water present)
Purity (HPLC Area%) 30.6% 68.5%

5

- 20 -
Summary of Oxidation Examples
A summary of the Examples for oxidation of LMEA to LG is set forth in the Table below.

Ex. No NaOCl: Substrate NaOCl Cone. Solvent Reac Time (hr.) Initial Temp
(°C) Peak Temp
(°C) Initial pH Final pH Isolation Method Work¬up pH Yield
as
Acid Yield
as
Salt
1 6.5:1 11.5% THF 2 24 32 12.71 7.57 THF Extraction 3.0 116% 107%
2 3.25:1 11.5% THF 2 24 26 9.89 7.61 THF Extraction 2.1 103% 95%
3 3.25:1 11.5% THF 2 25.4 26.9 10.3 7.8 THF Extraction 8.3 108% 99%
4 6.5:1 11.5% THF 2 24.8 30.2 11.56 7.24 Water
Drowning 2.6 77% 71%
5 3.25:1 11.5% THF 3 23 25.2 10.35 - Water Drowning 5.2 59% 55%
6 3.25 5% Water 21a 19.5 19.5 8.56 7.81 THF Extraction 2.5 114% 105%
a) Actual reaction time may be less.

A summary of the Examples of the oxidation of N-cocoylmethanolamide to N-cocoylglycine is set forth in the Table below.

Ex. No NaOCl: Substrate NaOCl
Cone. Solvent Reac Time (hr.) Initial Temp TO Peak
Temp
(°C) Initial pH Final pH Isolation Method Work¬up pH Yield
as
Acidb Yield
as
Saltb
7 3.25:1 11.5% Toluene 6 a 31 38 8.9 THF Extraction 2.2 84% 78%
8 3.25:1 11.5% Cyclo-hexane 16 a 38.5 41 6.2 THF Extraction 3.1 73% 67%
5 a) Actual reaction time may be less.
b) Assume CMEA and CG are each the corresponding 100% C-12 compounds.

Example 9. Oxidation of CMEA with 1.6 - 2.5 eq. of NaOCl in Water.
CMEA (6g) was suspended in water (150mL) and stirred for 30 min at high speeds using a mechanical stirrer. AA-TEMPO {0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 1.6-2.5 eq.) under vigorous stirring maintaining the temperature between 22 to 33 °C. Between additions, the pH was maintained around 8 - 9 by adding IN NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 6 hours at 65 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N KCl and the white solid product filtered and dried under high vacuum 5.45g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 2 below.
Example 10. Oxidation of CMEA with 2.3 - 3.2 eq. of NaOCl in Water.
CMEA (6g) was suspended in water (150mL) and stirred for 3D min at high speeds using a mechanical stirrer. AA-TEMPO (0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 2.3-3.2 eq.) under vigorous stirring maintaining the temperature between 22 to 33 °C. Between additions, the pH was maintained around 8 - 9 by adding IN

NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 8 hours at 60 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N HC1 and the white solid product filtered and dried under high vacuum 5.75g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 3 below.
Example 11. Oxidation of CMEA with 3.2 - 4.0 eq. of NaOCl in Water.
CMEA (6g) was suspended in water (150mL) and stirred for 30 min at high speeds using a mechanical stirrer. AA-TEMPO (0.101 g, 0.02 eq.) and KBr (0.113 g, 0.04 eq.) were added to the reaction mixture, followed by dropwise addition of NaOCl (10 to 14 %, 3.2-4 eq.) under vigorous stirring maintaining the temperature between 22 to 26 °C. Between additions, the pH was maintained around 8 - 9 by adding IN NaOH. The reaction progress was closely monitored by HPLC and continued for 24 hours until consumption of CMEA ceased. At this point, the reaction mixture was heated for 8 hours at 60 °C to ensure full conversion into cocoyl glycinate product. The mixture was acidified to pH 3 with 1 N HC1 and the white solid product filtered and dried under high vacuum 5.50g. A representative HPLC reaction profile demonstrating the conversion of CMEA to cocoyl glycinate is shown in Figure 4 below.

CLAIMS
1. A process for converting an alcohol comprising amide group to corresponding carboxylic acid in yield _>75% which process comprises reacting:
R1 - CONR2 (CH2)mOH
wherein R1 is linear or branched alkyl or alkenyl group having 7 to 22 carbon atoms; R2 is H, an alkyl or hydroxyalkyl group with 1 to 6 carbon atom(s); and m is an integer from 1 to 6,
with an oxidizing agent in the presence of a hindered nitroxide radical and optional co-catalyst, wherein the solvent is solely water and, in the presence of the oxidizing agent, oxidizing agent separates into water, and the amidoalcohol stays or partitions in a solid organic layer to thereby permit the high yields noted.
2. A process according to claim 1, wherein the alcohol comprising amide group is an alkanoylmonoalkanolamine.
3. A process according to claim 2, wherein the alkanoylmonoalkanolamine is lauroyl monoalkanolamide or cocomonoethanolamide.
4. A process according to claim 1, wherein the oxidizing agent is selected from the group consisting of chlorine, a hypochlorite, chloroisocyanuric acid and mixtures thereof.

5. A process according to claim 1 wherein the oxidizing agent is selected from the group consisting of Na03r, bromosuccinimide, bromoisocyanuric acid, peracids, oxone, H2O2 and mixture thereof.
6. A process according to claim 1, wherein oxidizing agent is present in amount from equimolar to 8 molar.
7. A process according to claim 1, wherein the nitroxide catalyst is 4-acetamido-TEMPO.
8. A process according to claim 1, where, in addition to hindered nitroxide radical co-catalyst is used.
9. A process according to claim 8, wherein co-catalyst is alkali metal halide or alkali earth metal halide.
10. A process according to claim 1, wherein solvents contain substantially no anti-oxidants.
11. A process according to claim 1, where base is additionally added to the reaction.
12. A process according to claim 1, wherein sufficient base is added to maintain pH above 6.
13. A process according to claim 1, wherein the oxidizing agent is chlorine or chlorine containing molecule, wherein the oxidizing agent is added and reaction given 30 minutes to 24 hours to reach completion and wherein

the resulting solution is heated for 1 to 24 hours at a temperature of at least 40°C to 100°C.
Dated this 16th day of December 2008

Documents:

2673-MUMNP-2008-ANNEXURE TO FORM 3(30-7-2012).pdf

2673-mumnp-2008-assignment.pdf

2673-MUMNP-2008-CLAIMS(AMENDED)-(30-7-2012).pdf

2673-MUMNP-2008-CLAIMS(MARKED COPY)-(30-7-2012).pdf

2673-mumnp-2008-claims.doc

2673-mumnp-2008-claims.pdf

2673-MUMNP-2008-CORRESPONDENCE(19-3-2010).pdf

2673-MUMNP-2008-CORRESPONDENCE(21-12-2012).pdf

2673-MUMNP-2008-CORRESPONDENCE(24-10-2011).pdf

2673-mumnp-2008-correspondence.pdf

2673-mumnp-2008-description(complete).doc

2673-mumnp-2008-description(complete).pdf

2673-mumnp-2008-drawing.pdf

2673-MUMNP-2008-EP DOCUMENT(30-7-2012).pdf

2673-mumnp-2008-form 1.pdf

2673-MUMNP-2008-FORM 13(9-2-2012).pdf

2673-MUMNP-2008-FORM 18(19-3-2010).pdf

2673-mumnp-2008-form 2(title page).pdf

2673-mumnp-2008-form 2.doc

2673-mumnp-2008-form 2.pdf

2673-MUMNP-2008-FORM 3(12-8-2011).pdf

2673-MUMNP-2008-FORM 3(15-2-2011).pdf

2673-MUMNP-2008-FORM 3(15-2-2012).pdf

2673-MUMNP-2008-FORM 3(16-12-2008).pdf

2673-MUMNP-2008-FORM 3(23-1-2013).pdf

2673-MUMNP-2008-FORM 3(24-2-2010).pdf

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2673-MUMNP-2008-FORM 3(8-8-2012).pdf

2673-mumnp-2008-form 3.pdf

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2673-mumnp-2008-pct-ib-306.pdf

2673-mumnp-2008-pct-ib-311.pdf

2673-mumnp-2008-pct-isa-210.pdf

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2673-MUMNP-2008-REPLY TO EXAMINATION REPORT(30-7-2012).pdf

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Patent Number

256167

Indian Patent Application Number

2673/MUMNP/2008

PG Journal Number

20/2013

Publication Date

17-May-2013

Grant Date

10-May-2013

Date of Filing

16-Dec-2008

Name of Patentee

HINDUSTAN UNILEVER LIMITED

Applicant Address

UNILEVER HOUSE, B.D. SAWANT MARG, CHAKALA, ANDHERI EAST, MUMBAI-400 099 MAHARASHTRA, INDIA

Inventors:

#	Inventor's Name	Inventor's Address
1	CHEN HANG	UNILEVER HOME & PERSONAL CARE USA, 40 MERRITT BOULEVARD, TRUMBULL, CONNECTICUT 06611,
2	ROSA JOSE GUILLERMO	UNILEVER HOME & PERSONAL CARE USA, 40 MERRITT BOULEVARD, TRUMBULL, CONNECTICUT 06611,
3	HARICHIAN BIJAN	UNILEVER HOME & PERSONAL CARE USA, 40 MERRITT BOULEVARD, TRUMBULL, CONNECTICUT 06611,

PCT International Classification Number

C07C231/12

PCT International Application Number

PCT/EP2007/056140

PCT International Filing date

2007-06-20

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	11/475824	2006-06-27	U.S.A.