Title of Invention

"PREPARATION OF DERIVATIZED DITHIOLS"

Abstract

Process for preparing a compound of the formula (I) wherein the R1 and R2 radicals are each independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aralkyl, phenyl, substituted phenyl, alkylaryl, and a heterocyclic ring having 4 to 8 carbon atoms including at least one nitrogen atom, and where n is an integer from 2 to 8, comprising the step of reacting a compound of the formula wherein R1 and R2 radicals are each as defined in the formula (I) and z-1 when Me1 is an alkali metal or ammonium ion and z=2 when Me is an alkaline earth metal ion, with a compound of the formula (III) wherein Me and Me are the same or different and are each monovalent metal ions or ammonium ions and n is as defined in the formula (I), wherein said step of reacting is performed in the presence of water, a carbonyl containing compound and an organic solvent, in a pH range of 7 to 14 at a reaction temperature of 0° to 90oC, until the compound of the formula (I) reaches a percent yield of at least 80% based on the salts of the formula (III), further wherein the amount of the compound of the formula (II) is 180 to 250 mol % based on the moles of the compound of the formula (III) used, the amount of the carbonyl containing compound is 5 to 600 mol % based on the moles of the compound of the formula (III) used, and the amount of the organic solvent is 2 to 100,000 parts by weight based on 100 parts by weight of the theoretical yield of the compound of the formula (I).

Full Text

WE CLAIM: 1. Process for preparing a compound of the formula (I) (Formula Removed) wherein the R1 and R2 radicals are each independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aralkyl, phenyl, substituted phenyl, alkylaryl, and a heterocyclic ring having 4 to 8 carbon atoms including at least one nitrogen atom, and where n is an integer from 2 to 8, comprising the step of reacting a compound of the formula (Formula Removed) wherein R1 and R2 radicals are each as defined in the formula (I) and z =1 when Me is an alkali metal or ammonium ion and z=2 when Me is an alkaline earth metal ion, with a compound of the formula (III) (Formula Removed) wherein Me and Me are the same or different and are each monovalent metal ions or ammonium ions and n is as defined in the formula (I), wherein said step of reacting is performed in the presence of water, a carbonyl containing compound and an organic solvent, in a pH range of 7 to 14 at a reaction temperature of 0 to 90 C, until the compound of the formula (I) reaches a percent yield of at least 80% based on the salts of the formula (III), further wherein the amount of the compound of the formula (II) is 180 to 250 mol % based on the moles of the compound of the formula (III) used, the amount of the carbonyl containing compound is 5 to 600 mol % based on the moles of the compound of the formula (III) used, and the amount of the organic solvent is 2 to 100,000 parts by weight based on 100 parts by weight of the theoretical yield of the compound of the formula (I). 2. The process as claimed in claim 1, wherein the organic solvent is used in an amount of 2 to 100 parts by weight based on 100 parts by weight of the theoretically yield expected of the compound of the formula (I) and the reaction temperature is in the range of 0 to 60° C, further wherein a portion of the compound of the formula (I) is found at the end of the reaction to be dissolved in the organic solvent and where the amount of the compound of the formula (I) dissolved in the organic solvent at the end of the reaction is at most 15 parts by weight based on 100 parts by weight of the compound of the formula (I). 3. The process as claimed in claim 1, wherein the organic solvent is used in an amount of 105 to 100,000 parts by weight based on 100 parts by weight of the theoretical yield expected of the compound of the formula (I) and the reaction temperature is in the range of 0° to 90° C, and wherein the compound of the formula (I) are found to be dissolved fully in the organic solvent at the end of the reaction, thereby forming a reaction solution. 4. The process as claimed in claim 3, wherein the resulting reaction solution, comprising the organic solvent, is contacted with a support and subsequently the organic solvent is evaporated. 5. The process as claimed in claim 4, wherein said support is at least one of silicate, clay earth, kaolin, siliceous earth, talc, chalk, metal oxide, metal carbonate, carbon black or silica.

Documents:

1304-DEL-2005-Abstract-(31-07-2012).pdf

1304-DEL-2005-Claims-(31-07-2012).pdf

1304-del-2005-Correspondence Others-(21-05-2008).pdf

1304-del-2005-Correspondence Others-(25-05-2012).pdf

1304-DEL-2005-Correspondence Others-(31-07-2012).pdf

1304-del-2005-Form-18-(21-05-2008).pdf

1304-del-2005-Form-3-(25-05-2012).pdf

1304-DEL-2005-GPA-(31-07-2012).pdf

1304-DEL-2005-Petition-137-(31-07-2012).pdf