Abstract A method of salt grinding of pigments wherein the material to be ground is milled with a salt, an organic conditioner, and larger particles such as balls, nails, or in a strong kneader for comminuting the pigment to the desired state of subdivision. This grinding mass is made into a smooth flowing suspension by addition of more organic conditioning agent rather than solvents, as heretofore. The suspension is then passed through a decanter type centrifuge resulting in a sediment fraction containing most of the salt, some pigment, and some organic conditioning agent, and a liquid fraction containing most of the pigment, some salt and conditioning agent. The sediment portion is returned to the grinding mechanism where it is combined with a new batch of unmilled pigment for a subsequent milling cycle, while the pigment is separated by filtration from the liquid portion after some addition of water and flocculating agents. The filtration and wash liquors are combined. After evaporation, these liquors are then used for thinning out of the milling mass of a subsequent batch.
In salt grinding of pigments, the improvement comprising (a) milling oversize crude organic pigment with an inorganic salt and an organic conditioner until a predetermined state of pigmentary quality is obtained; (b) dispersion of the above mixture in a dispersing medium to provide a smooth suspension; (c) separating the resulting suspension into a liquid phase consisting of properly sized pigment, conditioner, and some salt and a sediment phase comprising the major portion of the salt, conditioner, and a small part of the pigment; (d) returning the sediment phase to step a for a subsequent batch in a new grinding cycle with new unfinished pigment; (e) separating the pigment from said liquid phase by filtration after addition of some water and flocculating agent to form press cake; (f) washing the resulting press cake free of conditioning agent and salt with water; and (g) combining filtration liquor from step e and wash water from step f and evaporating the water from the conditioning agent leaving a mass of conditioning agent and some salt in the unit; wherein organic conditioner is used as the dispersing medium in step b.
Claim 2
Dependent Claim
186 words
In salt grinding of pigments, the improvement comprising (a) milling oversize crude organic pigment with an inorganic salt and an organic conditioner until a predetermined state of pigmentary quality is obtained; (b) dispersion of the above mixture in a dispersing medium to provide a smooth suspension; (c) separating the resulting suspension into a liquid phase consisting of properly sized pigment, conditioner, and some salt and a sediment phase comprising the major portion of the salt, conditioner, and a small part of the pigment; (d) returning the sediment phase to step a for a subsequent batch in a new grinding cycle with new unfinished pigment; (e) separating the pigment from said liquid phase by filtration after addition of some water and flocculating agent to form press cake; (f) washing the resulting press cake free of conditioning agent and salt with water; and (g) combining filtration liquor from step e and wash water from step f and evaporating the water from the conditioning agent leaving a mass of conditioning agent and some salt in the unit; wherein organic conditioner is used as the dispersing medium in step b.
Claim 3
Dependent Claim
15 words
The process of claim 1 wherein the pigment of claim 1 is a copper phthalocyanine.
Claim 4
Dependent Claim
28 words
The process of claim 1 wherein the conditioning agent employed for the grinding and dispersion step is an ethylene glycol, polyethylene glycol, or a mixture of these glycols.
Claim 5
Dependent Claim
26 words
The process of claim 1 wherein the separation of step (c) into a liquid phase and a sediment phase is accomplished by a decanter type centrifuge.
Claim 6
Dependent Claim
19 words
The process of claim 1 wherein the mass of (b) is heated before passing through a decanter type centrifuge.
Claim 7
Dependent Claim
16 words
The process of claim 1 wherein the dispersing medium is the mass resultant from step g.