Title of Invention

PROCESS FOR THE PREPARATION OF 2-METHYL 1,4-NAPHTHOQUINONE

Abstract

The present invention relates to a process for the preparation of 2-Methyl-l, 4-naphthoquinone (vitamin K3, "menadione"). The present invention particularly relates to a process for producing 2-Methyl-l, 4-naphthoquinone which is used as antihemoragic agent and in animal feed, by the oxidation of 2-Methylanpahthalene with hydrogen peroxide in the presence of acetic acid. The process involves oxidation of 2-methylnaphthalene with hydrogen peroxide in the presence of acetic acid and separating the 2-methyl-l, 4-naphthoquinone so obtained.

Full Text

PROCESS FOR PREPARATION OF 2-METHYL-l,4-NAPHTHOQUINONE Field of the invention The present invention relates to a process for the preparation of 2-Methyl-l,4-naphthoquinone (vitamin Ks, "menadione" ). The present invention particularly relates to a process for producing 2-Methyl-l,4-naphthoquinone which is used as antihemoragic agent and in animal feed, by the oxidation of 2-Methylnaphthalene with hydrogen peroxide in the presence of acetic acid. Background of the invention Oxidation is one of the major and industrially important processes and widely used in the synthesis of low and high volume chemicals and pharmaceutical industry. Furthermore, the traditional route of oxidation using mineral acids and inorganic oxides suffer from the disadvantages of high capital cost, reactor corrosion, formation of by product and the difficulty in the catalyst regeneration. In the recent times, scientists worldwide have been devoting their attention to the development of environmentally friendly catalysts and economically feasible routes. Oxidation of arenas is important in chemical industries, especially in agrochemical and pharmaceutical industries. Many oxidation and hydroxylation reactions were studied using zeolites and redoxmolecular sieves (Sheldon et al. Curr. Opin. Solid. State Mater. Sci. 1, 1996, 101; Sheldon et al. J. Mol. Catal. A 107, 1996, 75; Kumar et al. Synlett. 1995, 289; Arends et al. Angew. Chem. Int. Ed. Engl. 36, 1997, 1145). Oxidation of 2-Methylnaphthalene with a sulfuric acid solution of chromic acid was studied (Fieser, J. Biol. Chem.. 133, 1940, 391; Sheldon, Top. Curr. Chem.. 164, 1993, 21). However, in this stoichiometric oxidation about 18 kg of chromium containing waste is produced for 1 kg of product. Oxidation of 2-Methlynaphthalene was investigated in presence of acetic acid with hydrogen peroxide and methyl trioxo rhenium (Adam et al., Angew. Chem. Int. Ed.. 33, 1994, 2475; Herrmann et al., J. Mol. Catal. A Chemical. 138, 1999, 115). Oxidation of 2-Methylnaphthalene was carried over Pd-polystyrenesulfonic acid resin in the acetic acid with hydrogen peroxide (Yamaguchi et al., Chem. Lett.. 1985, 827). Metalloporphyrin catalyzed oxidation of 2-Methylnaphthalene by potassium monopersulfate was studied (Song et al., J. Ore. Chem.. 62, 1997, 673). The oxidation of 2-Methylnaphthalene has been carried out using ammonium persulfate as an oxidizing agent in the presence of cerium (IV) ammonium sulfate and silvernitrate in an emulsified solution (Skarzewski, Tetrahedron. 40, 1984, 4997). The synthesis of vitamin K3 from different starting materials like 1-naphthol, 1, 4-naphthoquinone was examined using organic oxidizing agents (Rama Rao et al. Indian J. Chem. 24 B, 1985, 233). Oxidation of 2-Methylnaphthalene using hydrogen peroxide in the presence of acid catalysts have been cooked in patents (Sugano et al. Ger. Offen DE. 2341463, 1974; Takanobu et al. Japanese kokai 77, 1977, 108959; Baba et al. Japanese kokai 76, 1976, 50147). The drawbacks of using inorganic oxidants and mineral acids as given in the referred work are: (I) Catalyst can not be reused, (ii) Disposal of acid is not environmentally safe and it is not economical, (iii) Low selectivity is frequently observed, (iv) Corrosion of the reaction vessel and reactors, (v) Not easy to handle and (vi) High inventory of the catalyst. Objects of the invention The main object of the present invention is to develop low cost and ecofriendly route for the oxidation of 2-Methylnaphthalene. Another object of the present invention is to provide a process for the preparation of 2-Methyl-1, 4-naphthoquinone. Summary of the invention Accordingly, the present invention relates to a process for the preparation of 2-Methyl-1, 4-naphthoquinone, said process comprising oxidizing 2-methylnaphthalene with hydrogen peroxide in a molar ratio of 1:2 to 1:12 in the presence of acetic acid of concentration in the range of 5-17N at temperature in the range of 60-100°C for a time period of 1-3 hrs and separating the 2-methyl-l, 4-naphthoquinone so obtained. In one embodiment of the invention, the reaction is carried out in the absence of solid catalysts are used. In another embodiment of the present invention, the reaction is carried out in a temperature range from 60 to 100°C. In another embodiment of the present invention, the reaction is carried out for a period of 1-3 hrs. Detailed description of the invention The present invention provides a process for oxidization of 2-Methylnaphthalene with hydrogen peroxide in acetic acid. The reaction of the invention avoids the use of solid acid catalysts in the preparation of 2-Methyl-l, 4-naphthoquinone. The following examples are given by the way of illustration and therefore should not be construed as to limit the scope of the present invention. EXAMPLE 1 20 ml of acetic acid was taken in 50 ml round bottom flask and I g of 2-Methylnaphthalene added and kept on a magnetic stirrer. The reaction mixture was heated to 100°C. After reaching 100°C hydrogen peroxide was added slowly and allowed the reaction mixture for 3 hrs at 100°C. The reaction mixture was analysed using a CHEJvflTO 8510 Gas Chromatography using 20 % SE-30 column coupled with flame ionization detector for product distribution. A typical Gas Chromatography - Mass spectral fragmentation pattern and Proton Nuclear Magnetic Resonance spectra of. the products, 'H NMR proves that the product obtained was 2-Methyl-I,4-naphthoquinone. The reaction was carried out using different molar ratios of 2-Methylnaphthalene to hydrogen peroxide (30%) as 1:2, 1:4, 1:6, 1:8 and 1:10. Product was analyzed and the conversion and selectivity are given in Table 1. Table - 1 Conversion and selectivities using, different molar ratios of 2-methylnaphthalene to hydrogen peroxide (30%) (Table Removed) EXAMPLE 2 20 ml of acetic acid was taken in 50 ml round bottom flask and 1 g of 2-Methylnaphthalene added and kept on a magnetic stirrer. The reaction mixture was heated to 100°C. After reaching 100°C hydrogen peroxide was added slowly and allowed the reaction mixture for 3hrs at 100°C. The reaction was carried out using 5 to 17 N concentrations of acetic acid. Product was analyzed and the conversion and selectivity are given in Table 2. Table- 2 Conversion and selectivities with concentration of acetic acid (Table Removed) EXAMPLE 3 20 ml of acetic acid was taken in 50 ml round bottom flask and I g of 2-Methylnaphthalene added and kept on a magnetic stirrer. The reaction mixture was heated to 100°C: After reaching 100°C, hydrogen peroxide was added slowly and allowed the reaction mixture for 3hrs at 100°C. The reaction was carried out using 10 to 50 % concentration of hydrogen peroxide. Product was analyzed and the conversion and selectivity are given in the Table 3. Table - 3 Conversion and selectivities with concentration of hydrogen peroxide (Table Removed) EXAMPLE 4 20 ml of acetic acid was taken in 50 ml round bottom flask and 1 g of 2-Methylnaphthalene added and kept on a magnetic stirrer. The reaction mixture was heated to 100°C. After reaching 100°C hydrogen peroxide was added slowly and allowed the reaction mixture for heating at 100°C. The reaction was carried out for different time periods ranging from 30 min to 240 min. Products were analyzed and the conversion and selectivity are given in the Table 4. Table - 4 Conversion and selectivities with the variation in the time (Table Removed) EXAMPLE 5 1 g of 2-Methylnaphthalene taken in 50 ml round bottom flask and acetic acid was added and was kept on a magnetic stirrer. The reaction mixture was heated to 100°C. After reaching 100°C hydrogen peroxide was added slowly and allowed the reaction mixture for 3hrs at 100°C. The reaction was carried out by changing the amount of acetic acid from 5 to 20 ml. Product was analyzed and the conversion and selectivity are given in the Table 5. (Table Removed) EXAMPLE 6 20 ml of acetic acid was taken in 50 ml round bottom flask and 1 g of 2-Methylnaphthalene added and kept on a magnetic stirrer and hydrogen peroxide was added slowly and allowed the reaction mixture for 3hrs while stirring. The reaction was carried out by varying the reaction temperature from 40 to 100°C. Product was analyzed and the conversion and selectivities are given in the Table 6. Table- 6 Conversion and selectivities with reaction temperature (Table Removed) The main advantages of the present invention are: oxidation of 2-Methylnaphthalene to 2-Methyl-l,4-naphthoquinone with hydrogen peroxide in acetic acid without the use of solid catalyst is being reported for the first time. Also, this method provides the following advantages compared with the conventional process (i) high conversion and selectivity are frequently observed, (ii) no waste is produced which is an ecofriendly process, (iii) do not corrode reaction vessel or reactors and (iv) it is a very economical process as there is no involvement of solid catalysts. In view of the above, it will be seen that several advantages of the invention are achieved and other advantageous results attained. As various changes could be made in the above methods and compositions without departing from the scope of the invention, it is intended that all matter contained in the above description shall be interpreted as illustrative and not in a limiting sense. We Claim: 1. A process for the preparation of 2-Methyl-l, 4-naphthoquinone, said process comprising oxidizing 2-methylnaphthalene with hydrogen peroxide in a molar ratio of 1:2 to 1:12 in the presence of acetic acid of concentration in the range of 5-17N at temperature in the range of 60-100°C for a time period of l-3hrs and separating the 2-methyl-1, 4-naphthoquinone so obtained. 2. A process as claimed in claim 1 wherein the oxidation is carried out in the absence of a solid catalyst. 3. A Process for preparation of 2-methyl-l, 4-naphthoquinone, substantially as herein described with reference to the examples and drawings accompanying this specifications.

Documents:

01448-delnp-2003-abstract.pdf

01448-delnp-2003-claims.pdf

01448-delnp-2003-correspondence-others.pdf

01448-delnp-2003-description (complete)-21-08-2008.pdf

01448-delnp-2003-description (complete).pdf

01448-delnp-2003-form-1.pdf

01448-delnp-2003-form-18.pdf

01448-delnp-2003-form-2.pdf

01448-delnp-2003-form-3.pdf

1448-DELNP-2003-Abstract-(21-08-2008).pdf

1448-DELNP-2003-Claims-(21-08-2008).pdf

1448-DELNP-2003-Correspondence-Others-(21-08-2008).pdf

1448-DELNP-2003-Form-2-(21-08-2008).pdf

1448-DELNP-2003-Form-3-(21-08-2008).pdf

1448-DELNP-2003-Petition-137-(21-08-2008).pdf