Pigment conditioning and vehicle flushing process

Claim 2

A process for manufacturing pigmented oleoresinous coating vehicles comprising the steps of; partially conditioning a crude organic pigment by dry milling to an extent substantially less than the amount of milling required to develop full pigmentary strength; providing an aqueous slurry of the partially conditioned pigment; flushing the pigment from an aqueous slurry into a soft oleoresinous vehicle by mixing the aqueous pigment slurry with the vehicle and a volatile organic liquid breaching agent which is essentially immiscible with water under the flushing conditions and which is active to develop pigmentary qualities by contacting the pigment during flushing, said breaching agent being present in an amount at least about 1 part by weight per 100 parts of dry pigment; separating water from the flushed mass mixture of pigment, vehicle and breaching agent; separating the volatile organic breaching agent from the flushed mass by evaporation, thereby producing a pigmented oleoresinous vehicle having pigmentary qualities substantially equal to that produced by incorporating a fully conditioned pigment into the vehicle.

Claim 3

The process of claim 1 wherein the breaching agent is selected from the class consisting of paraffinic and cycloaliphatic hydrocarbons having at least 5 carbon atoms, aromatic hydrocarbons having 6 to 10 carbon atoms, halogenated hydrocarbons having 1 to 10 carbon atoms, alkyl ethers having 4 to 14 carbon atoms, alkyl esters of alkanoic acids having a total of 4 to 12 carbon atoms, and liquid mixtures of these organic breaching agents with one another.

Claim 4

The process of claim 2 wherein the pigment consists essentially of copper phthalocyanine.

Claim 5

The process of claim 1 wherein the breaching agent is added in an amount about equal to 10 to 300 parts per 100 parts by weight of dry pigment.

Claim 6

The process of claim 1 wherein the breaching agent is added to the aqueous slurry and oleoresinous vehicle at the beginning of the flushing step.

Claim 7

The process of claim 1 wherein the breaching agent is added to the aqueous slurry and oleoresinous vehicle after flushing of the pigment into the vehicle has broken the flushing mixture into aqueous and orgnaic phases.

Claim 8

The process of claim 1 wherein the organic pigment is selected from phthalocyanines, quinacridones, dioxazines, perylenes, indathrones and vat pigments and mixtures of these pigments.

Claim 9

In the process wherein an organic crystalline crude pigment is conditioned to essentially full pigmentary strength by partial conditioning of the crude pigment in an attrition mill and treatment of the partially milled pigment with a breaching agent to promote further conditioning; the improvement which comprises: a. treating the partially milled pigment with a dilute aqueous mineral acid solution; b. flushing and further conditioning the wet acid-treated pigment by transferring the pigment into an organic vehicle in which the pigment is dispersible; and contacting the pigment during the flushing step with a conditioning amount of at least 1 part by weight breaching agent per 100 parts dry pigment; said breaching agent consisting essentially of one or more volatile organic breaching liquids selected from aromatic hydrocarbons having 6 to 10 carbon atoms, aliphatic and cyclo-aliphatic hydrocarbons having at least 5 carbon atoms, halogenated hydrocarbons having 1 to 10 carbon atoms, alkyl ethers having 4 to 12 carbon atoms, alkyl esters of alkanoic acids having a total of 4 to 12 carbon atoms, and liquid mixtures of these organic breaching agents with one another; said breaching (agents) liquid boiling below about 200°C and having a maximum solubility in water of about 5% by weight at room temperature; and c. separating the pigmented organic vehicle from the agueous phase formed during flushing, said pigmented organic vehicle having a tint strength substantially equal to or greater than that obtained by milling the crude pigment to substantially full pigmentary strength and flushing the fully milled pigment into the organic vehicle without addition of the breaching agent.

Claim 10

In the process wherein an organic crystalline crude pigment is conditioned to essentially full pigmentary strength by partial conditioning of the crude pigment in an attrition mill and treatment of the partially milled pigment with a breaching agent to promote further conditioning; the improvement which comprises: a. treating the partially milled pigment with a dilute aqueous mineral acid solution; b. flushing and further conditioning the wet acid-treated pigment by transferring the pigment into an organic vehicle in which the pigment is dispersible; and contacting the pigment during the flushing step with a conditioning amount of at least 1 part by weight breaching agent per 100 parts dry pigment; said breaching agent consisting essentially of one or more volatile organic breaching liquids selected from aromatic hydrocarbons having 6 to 10 carbon atoms, aliphatic and cyclo-aliphatic hydrocarbons having at least 5 carbon atoms, halogenated hydrocarbons having 1 to 10 carbon atoms, alkyl ethers having 4 to 12 carbon atoms, alkyl esters of alkanoic acids having a total of 4 to 12 carbon atoms, and liquid mixtures of these organic breaching agents with one another; said breaching (agents) liquid boiling below about 200°C and having a maximum solubility in water of about 5% by weight at room temperature; and c. separating the pigmented organic vehicle from the agueous phase formed during flushing, said pigmented organic vehicle having a tint strength substantially equal to or greater than that obtained by milling the crude pigment to substantially full pigmentary strength and flushing the fully milled pigment into the organic vehicle without addition of the breaching agent.

Claim 11

A process for manufacturing pigmented organic vehicles comprising the steps of: milling a crude phthalocyanine pigment to an extent substantially less than that amount of milling required to develop full pigmentary properties: slurrying the partially conditioned pigment with a dilute aqueous mineral acid to extract impurities; flushing and further conditioning the pigment during the flushing step by mixing the aqueous pigment with a hydrophobic organic vehicle and at least 1 part (sufficient) organic liquid breaching agent per 100 parts by weight of dry pigment in sufficient amount to complete conditioning of the pigment, said breaching agent being essentially immiscible with water under the flushing conditions and being active to develop pigmentary qualities by contacting the pigment during flushing; and separating water from the flushed mass mixture of pigment, vechicle and breaching agent, thereby producing a pigmented vehicle having pigmentary strength substantially equal to that produced by incorporating a fully conditioned pigment into the vehicle.

Claim 12

A process for manufacturing pigmented organic vehicles comprising the steps of: milling a crude phthalocyanine pigment to an extent substantially less than that amount of milling required to develop full pigmentary properties: slurrying the partially conditioned pigment with a dilute aqueous mineral acid to extract impurities; flushing and further conditioning the pigment during the flushing step by mixing the aqueous pigment with a hydrophobic organic vehicle and at least 1 part (sufficient) organic liquid breaching agent per 100 parts by weight of dry pigment in sufficient amount to complete conditioning of the pigment, said breaching agent being essentially immiscible with water under the flushing conditions and being active to develop pigmentary qualities by contacting the pigment during flushing; and separating water from the flushed mass mixture of pigment, vechicle and breaching agent, thereby producing a pigmented vehicle having pigmentary strength substantially equal to that produced by incorporating a fully conditioned pigment into the vehicle.

Claim 13

The process of claim 9 wherein the breaching agent is selected from liquid aliphatic, cycloaliphatic and aromatic hydrocarbons, halogenated aliphatic hydrocarbons, alkyl esters of alkanoic acids, and alkyl ethers having a boiling point not greater than 200° C, viscosity of about 0.2 to 3 centipoises, and a solubility in water at room temperature not greater than 5% by weight.

Claim 14

The process of claim 10 wherein the pigment consists essentially of phthalocyanine pigments containing statistically less than one substituent ring group per molecule.

Claim 15

The process of claim 9 wherein the breaching agent is added in an amount about equal to at least 10 parts per 100 parts by weight of dry pigment.

Claim 16

The process of claim 9 wherein the breaching agent is added to the aqueous slurry and vehicle at the beginning of the flushing step.

Claim 17

The process of claim 9 wherein the breaching agent is added to the aqueous slurry and vehicle after flushing of the pigment into the vehicle has broken the flushing mixture into aqueous and organic phases.

Claim 18

The process of claim 9 wherein the liquid breaching agent is a solvent for the organic vehicle and remains in the flushed mass as an integral part of the pigmented vehicle product.

Claim 19

The process of claim 9 wherein the milling step is carried out in a ball mill with grinding elements having an average size of about 0.25 to 2 cm in the presence of inorganic salt grinding aid, said grinding aid being used in an amount from 1.5 to 4.0 parts salt per part pigment.

Claim 20

The process of claim 16 wherein the milling time is less than one half of the time required to develop fully conditioned pigment by milling.