Amide waxes

Claim 2

A process for preparing organic amide waxes having at least two amide groups of formula --CO--NH-- per molecule derived from reaction between carboxylic acid groups and isocyanate groups, which comprises heating to an elevated temperature at least one monocarboxylic acid of the formula R 1 --COOH wherein R 1 is a linear or branched, saturated or unsaturated aliphatic hydrocarbon radical of 5 to 21 carbon atoms, introducing to the acid at least one organic isocyanate having the general formula NCO--R.sub.2 --A wherein R 2 is selected from the group consisting of straight chained, branch chained and cyclic aliphatic hydro-carbon radicals of at least 6 carbon atoms, and aromatic hydrocarbon radicals; wherein the aliphatic or aromatic hydrocarbon radical may be unsubstituted or substituted with one or more of lower alkyl of 1 to 8 carbon atoms, lower alkoxy of 1 to 8 carbon atoms, aryl and halogen; and A is selected from --NCO and --Alk--(NCO--R 3 --CH 2 --) N --R 4 --NCO wherein Alk is a single bond or an aliphatic hydrocarbon radical of 1 to 4 carbon atoms, n is 0 or more and R 3 and R 4 which may be the same or different are selected from the same group as R 2 and may be the same or different as R 2 , and reacting the acid and isocyanate together with elimination of carbon dioxide, said acid and isocyanate being reacted in amounts such that the number of carboxlic acid groups is at least approximately equal to the number of isocyanate groups, and the carboxylic acid groups are in an excess up to completion of amide group formation.

Claim 3

A process for preparing organic amide waxes free of isocyanate groups and having at least two amide groups of formula --CO--NH-- per molecule derived from reaction between carboxlic acid groups and isocyanate groups which comprises: heating at least one fatty acid having from 6 to 22 carbon atoms to an elevated temperature, not higher than the boiling point, to form a molten fatty acid phase, slowly adding to the acid, with stirring, at least one organic isocyanate, and reacting the acid with the isocyanate, with elimination of carbon dioxide, in the resulting reaction mixture containing an excess of said acid, to form the amide wax, said isocyanate having the general formula NCO--R.sub.2 --A wherein R 2 is selected from the group consisting of straight chained, branched and cyclic aliphatic hydrocarbon radicals of at least 6 carbon atoms, phenyl and naphthyl; wherein the phenyl, nahthyl or aliphatic hydrocarbon radical may be unsubstituted or substituted with one or more of lower alkyl of 1 to 8 carbon atoms, lower alkoxy of 1 to 8 carbon atoms, aryl and halogen; and A is selected from --NCO and --Alk--(NCO--R 3 --CH 2 --) n --R 4 --NCO wherein Alk is a single bond or an aliphatic hydrocarbon radical of 1 to 4 carbon atoms, n is 0 or more and R 3 and R 4 which may be the same or different are selected from the same group as R 2 and may be the same or different as R 2 ; and continuing the slow addition of the isocyanate to the reaction mixture until the number of isocyanate groups added is at least approximately equal to the original number of carboxylic acid groups such that said acid groups are in an excess up to completion of said amide group formation.

Claim 4

A process for preparing organic amide waxes free of isocyanate groups and having at least two amide groups of formula --CO--NH-- per molecule derived from reaction between carboxlic acid groups and isocyanate groups which comprises: heating at least one fatty acid having from 6 to 22 carbon atoms to an elevated temperature, not higher than the boiling point, to form a molten fatty acid phase, slowly adding to the acid, with stirring, at least one organic isocyanate, and reacting the acid with the isocyanate, with elimination of carbon dioxide, in the resulting reaction mixture containing an excess of said acid, to form the amide wax, said isocyanate having the general formula NCO--R.sub.2 --A wherein R 2 is selected from the group consisting of straight chained, branched and cyclic aliphatic hydrocarbon radicals of at least 6 carbon atoms, phenyl and naphthyl; wherein the phenyl, nahthyl or aliphatic hydrocarbon radical may be unsubstituted or substituted with one or more of lower alkyl of 1 to 8 carbon atoms, lower alkoxy of 1 to 8 carbon atoms, aryl and halogen; and A is selected from --NCO and --Alk--(NCO--R 3 --CH 2 --) n --R 4 --NCO wherein Alk is a single bond or an aliphatic hydrocarbon radical of 1 to 4 carbon atoms, n is 0 or more and R 3 and R 4 which may be the same or different are selected from the same group as R 2 and may be the same or different as R 2 ; and continuing the slow addition of the isocyanate to the reaction mixture until the number of isocyanate groups added is at least approximately equal to the original number of carboxylic acid groups such that said acid groups are in an excess up to completion of said amide group formation.

Claim 5

A process according to claim 2, wherein said elevated temperature is from about 160° C. to about 240° C. and the reaction is complete in 30 minutes to 4 hours; the fatty acid and isocyanate being reacted in amounts such that the amide wax contains not more than about 2% by weight of free acid.

Claim 6

A process according to claim 3, including the step of grinding the amide wax obtained to a powder having a particle size of about 5 to about 60 microns.

Claim 7

A process according to claim 3, wherein said reaction mixture is non-aqueous and free of solvent for said acid and isocyanate.

Claim 8

A process according to claim 5, wherein said at least one fatty acid contains 10 to 18 carbon atoms.

Claim 9

A process as defined in claim 1, wherein said at least one acid is selected from the fatty acids.

Claim 10

A process as defined in claim 7, wherein said at least one acid is a commercial grade of stearic acid.

Claim 11

A process as defined in claim 7, in which the fatty acid is commercial stearic acid and the isocyanate is a mixture of a polymethylene polyphenylisocyanate and methylene bisphenylisocyanate.

Claim 12

A process as defined in claim 9, in which said mixture contains about 50% by weight of each of said isocyanates.

Claim 13

A process as defined in claim 10, wherein said polyphenylisocyanate has the formula: NCO--R--CH.sub.2 --(NCO--R--CH.sub.2 --).sub.n --R--NCO wherein R is phenyl and n is 2.

Claim 14

A process as defined in claim 11, carried out at a temperature of about 225° C.

Claim 15

A process as defined in claim 1, comprising reacting a commercial grade of stearic acid with methylene bisphenylisocyanate.

Claim 16

A process, as defined in claim 13, carried out at a temperature of about 240° C.

Claim 17

A process as defined in claim 1, comprising reacting a commercial grade of stearic acid and a polymethylene polyphenylisocyanate represented by the structure NCO--R--CH.sub.2 --(NCO--R--CH.sub.2).sub.n --R--NCO where n is a number of one or more and R is a phenyl group.

Claim 18

A process as defined in claim 1, comprising reacting commercial grade stearic acid with a mixture of 2,4- and 2,6-toluene diisocyanate.

Claim 19

A process as defined in claim 1 comprising reacting commercial grade stearic acid with hexamethylene diisocyanate.

Claim 20

A process as defined in claim 1, wherein said at least one monocarboxylic acid is selected from the group consisting of the following acids: ______________________________________ Saturated Unsaturated ______________________________________ caprylic oleic capric linoleic lauric linolenic myristic eicosenoic palmitic lauroleic margaric myristoleic stearic palmitoleic arachidic gadoleic behenic erucic pelargonic elaeostearic isostearic licanic neodecanoic arachidonic 2-ethyl hexoic lignoceric caproic pentadecanoic ______________________________________

Claim 21

A process as defined in claim 1, wherein said at least one isocyanate is an aromatic diisocyanate selected from the group consisting of: toluene diisocyanate, bitolylene diisocyanate, dianisidine diisocyanate, p,p'-diphenylmethane diisocyanate o,p'-diphenylmethane diisocyanate 1-chloro-2,4-phenylene diisocyanate o,m and p-phenylene diisocyanate dichloroxenylene diisocyanate 2,4-toluene diisocyanate 2,6-toluene diisocyanate 2,2', 5,5'-tetramethyl-4,4'-biphenylene diisocyanate 4,4'-methylenebis (2-methylphenyl isocyanate) 1,5-naphthylene diisocyante 4,4-diphenylisopropylidine diisocyanate tolidine diisocyanate, xylylene diisocyanate, and diphenylxenylene diisocyanate.

Claim 22

A process as defined in claim 1, wherein said isocyanate is selected from polymethylene polyphenylisocyanate and polymethylene polycyclohexylisocyanate.

Claim 23

A process as defined in claim 1, wherein said isocyanate is an aliphatic diisocyanate selected from 1,6-hexamethylene diisocyanate methylcyclohexylene diisocyanate dicyclohexylmethane diisocyanate trimethylhexamethylene diisocyanate 3-isocyanate methyl-3,5-trimethyl cyclohexyl isocyanate 2,2,4(2,4,4)-trimethylhexamethylene diisocyanate.

Claim 24

A process as defined in claim 1, wherein said isocyanate is a dimer acid diisocyanate derived from dimerized linoleic acid.

Claim 25

A process as defined in claim 1, wherein said isocyanate is selected from isocyanates having a symmetrical structure.

Claim 26

A process as defined in claim 1, carried out at an elevated temperature effective to decompose an intermediate acid anhydride formed in the course of the reaction thereby avoiding formation of lumps.