Process for making quinacridone and its derivatives

Claim 2

A process for making quinacridone and its derivatives which comprises heating a 2,5-diarylaminoterephthalic acid and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono-or di-sulfonic acids of benzene, toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid; ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of 2,5-diaryl-aminoterephthalic acid and the organic liquid present in an amount of at least about 2 parts by weight per part of ethylene glycol, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 3

A process for making a quinacridone of the following formula: ##STR2## which comprises heating a 2,5-diarylaminoterephthalic acid of the following formula: ##STR3## wherein R 1 , R 2 , R 3 , R 4 , R 6 , R 7 , R 8 , R 9 can be the same or different and are selected from the group consisting H, alkyl, halogen, trifluoromethyl, alkoxy, carboxy, carboalkoxy, sulfonic acid, nitro, amino, alkylamino, mercapto, alkylmercapto, arylazo and aryl; and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono-and di-sulfonic acids of benzene, toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid; the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of 2,5-diarylaminoterephthalic acid and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 4

A process for making a quinacridone of the following formula: ##STR2## which comprises heating a 2,5-diarylaminoterephthalic acid of the following formula: ##STR3## wherein R 1 , R 2 , R 3 , R 4 , R 6 , R 7 , R 8 , R 9 can be the same or different and are selected from the group consisting H, alkyl, halogen, trifluoromethyl, alkoxy, carboxy, carboalkoxy, sulfonic acid, nitro, amino, alkylamino, mercapto, alkylmercapto, arylazo and aryl; and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono-and di-sulfonic acids of benzene, toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid; the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of 2,5-diarylaminoterephthalic acid and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 5

The process of claim 2 wherein the organic liquid is present in an amount of about 2 to about 40 parts by weight per part of ethylene glycol.

Claim 6

The process of claim 2 wherein the organic liquid is perchloroethylene.

Claim 7

The process of claim 2 wherein the organic liquid is selected from the group consisting of o-dichlorobenzene, trichlorobenzene, chlorobenzene, benzene, toluene, ortho, meta and paraxylene or mixtures thereof.

Claim 8

The process of claim 2 wherein the 2,5-diarylaminoterephthalic acid is 2,5-di-p-toluidinoterephthalic acid and the product is 2,9-dimethylquinacridone.

Claim 9

The process of claim 2 wherein the 2,5-diarylaminoterephthalic acid is 2,5-di-p-chloroanilinoterephthalic acid and the product is 2,9-dichloroquinacridone.

Claim 10

The process of claim 2 wherein the 2,5-diarylaminoterephthalic acid contains two identical arylamino groups selected from the group consisting of p-fluoroanilino, p-trifluoromethylanilino, p-carboxyanilino, p-carbomethoxyanilino, p-carboethoxyanilino, m-chloroanilino, o-chloroanilino, m-methylanilino, o-methylanilino and anilino and the product is a symmetrically substituted quinacridone.

Claim 11

The process of claim 2 wherein the 2,5-diarylaminoterephthalic acid contains two dissimilar arylamino groups selected from the group consisting of p-fluoroanilino, p-trifluoromethylanilino, p-carboxyanilino, p-carbomethoxyanilino, p-carboxyethoxyanilino, m-chloroanilino, o-chloroanilino, m-methylanilino, o-methylanilino and anilino and the resulting product is an unsymmetrically substituted quinacridone.

Claim 12

A process for making unsubstituted gamma quinacridone which comprises heating 2,5-dianilioterephthalic acid and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono- or di-sulfonic acids of benzene toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid, the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of 2,5-dianilinoterephthalic acid and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, in the presence of finely divided unsubstitued quinacridone, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 13

A process for making unsubstituted gamma quinacridone which comprises heating 2,5-dianilioterephthalic acid and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono- or di-sulfonic acids of benzene toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid, the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of 2,5-dianilinoterephthalic acid and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, in the presence of finely divided unsubstitued quinacridone, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 14

The process of claim 10 wherein the amount of finely divided unsubstituted quinacridone is at least about 0.001 part per part of 2,5-dianilinoterephthalic acid.

Claim 15

The process of claim 10 wherein the organic liquid is present in an amount of about 2 to about 40 parts by weight per part of ethylene glycol.

Claim 16

The process of claim 12 wherein the organic liquid is perchloroethylene.

Claim 17

A process for making substantially solid solutions of quinacridone mixtures being characterized in that the X-ray diffraction pattern thereof is different from the sum of the X-ray diffraction patterns of the component quinacridones, which comprises heating a mixture of 2,5-diarylaminoterephthalic acids and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono- or di-sulfonic acids of benzene, toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid; the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of the 2,5-diarylaminoterephthalic acid mixture and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 18

A process for making substantially solid solutions of quinacridone mixtures being characterized in that the X-ray diffraction pattern thereof is different from the sum of the X-ray diffraction patterns of the component quinacridones, which comprises heating a mixture of 2,5-diarylaminoterephthalic acids and an acid catalyst in a two phase liquid system, comprising ethylene glycol and an organic liquid which is immiscible with water and ethylene glycol, wherein the acid catalyst is selected from the group consisting of the mono- or di-sulfonic acids of benzene, toluene, xylene, paradichlorobenzene, naphthalene, nitrobenzene and chloroparaxylene, perchloric acid and methanesulfonic acid; the ethylene glycol is present in an amount of about 0.25 to 4 parts by weight per part of the 2,5-diarylaminoterephthalic acid mixture and the organic liquid is present in an amount of at least about 2 parts by weight per part of ethylene glycol, at a temperature sufficient to remove by-product water from the liquid system by vaporization.

Claim 19

The process of claim 14 wherein the organic liquid is present in an amount of about 2 to about 40 parts by weight per part of ethylene glycol.

Claim 20

The process of claim 14 wherein the organic liquid is perchloroethylene.

Claim 21

The process of claim 14 wherein the mixture of 2,5-diarylaminoterephthalic acids comprises 2,5-dianilinoterephthalic acid and at least one 2,5-diarylaminoterephthalic acid selected from the group consisting of 2,5-di-p-chloroanilinoterephthalic acid, 2,5-di-p-toluidinoterephthalic acid, 2,5-di-o-chloroanilinoterephthalic acid and 2,5-di-o-toluidinoterephthalic acid.

Claim 22

The process of claim 14 wherein the mixture of 2,5-diarylaminoterephthalic acids comprises 2,5-dianilinoterephthalic acid and 2,5-di-p-toluidinoterephthalic acid.

Claim 23

The process of claim 1 wherein the by-product water is continuously removed along with ethylene glycol and said organic liquid, and said organic liquid is returned to the system after its separation from water and ethylene glycol.

Claim 24

The process of claim 2 wherein the by-product water is continuously removed along with ethylene glycol and said organic liquid, and said organic liquid is returned to the system after its separation from water and ethylene glycol.

Claim 25

The process of claim 10 wherein the by-product water is continuously removed along with ethylene glycol and said organic liquid, and said organic liquid is returned to the system after its separation from water and ethylene glycol.

Claim 26

The process of claim 14 wherein the by-product water is continuously removed along with ethylene glycol and said organic liquid, and said organic liquid is returned to the system after its separation from water and ethylene glycol.