Aqueous ferrous waste conversion process

Claim 2

A process for the treatment of an aqueous ferrous sulfate waste stream, the sulfuric acid in said stream having been at least partially neutralized to make a gypsum product which gypsum product is separated therefrom, which comprises: turbulently mixing said at least partially neutralized stream with a recycled flow of coarser sludge solids from a later stage of the process, impalpable calcium carbonate selected from the group consisting of limestone, aragonite, oyster shell or mixtures thereof in at least about 3% stoichiometric excess, and molecular oxygen gas in substantial excess of the stoichiometric proportions required for converting the ferrous iron present in said stream into ferric iron in a slurry reaction zone until virtually complete sludging at a temperature of at least about 10° C. of the iron content of said stream takes place; classifying the resulting sludge into a coarser solids fraction of which at least about 10% by weight has an average particle size of greater than about 44 microns and an aqueous suspension of finer sludge solids; returning between about 10% and 70% by weight of the coarser solids fraction as said recycled flow; separating said finer sludge solids from said aqueous suspension thereof; and disposing of the remainder of said aqueous suspension as effluent.

Claim 3

The process of claim 1 wherein said reaction zone is a multiplicity of slurry reaction zones communicating serially with each other.

Claim 4

The process of claim 2 where the oxygen is in the form of air and in a proportion of at least about 10-100 times the stoichiometric, the calcium carbonate proportion is about 1.03-1.4 times the stoichiometric, and the superficial residence time of said reaction zones is at least about an hour.

Claim 5

The process of claim 3 wherein the unrecycled portion of said coarser solids fraction is dewatered by self-drainage, and said unrecycled portion amounts to about half of said fraction on a dry weight basis.

Claim 6

The process of claim 3 wherein the unrecycled portion of said coarser solids fraction is dewatered by filtration, and said unrecycled portion amounts to about half of said coarser solids fraction on a dry weight basis.

Claim 7

The process of claim 1 wherein between about 10% and 90% by weight of said coarser solids fraction has a particle size of greater than about 44 microns.

Claim 8

The process of claim 6, wherein between about 40% and 60% by weight of said coarser solids fraction has a particle size of greater than about 44 microns.

Claim 9

The process of claim 1 wherein the calcium carbonate used is aragonite, said waste stream originates from a sulfate process for producing titanium dioxide, and the free sulfuric acid therein is substantially completely neutralized and gypsum separated therefrom before said stream is subjected to the sludging operation, said waste stream containing not more than about 15 g/l of gypsum fines which enter the process.

Claim 10

The process of claim 1 wherein the calcium carbonate used is oyster shell, said waste stream originates from a sulfate process for producing titanium dioxide, and the free sulfuric acid therein is substantially completely neutralized and gypsum separated therefrom before said stream is subjected to the sludging operation, said waste stream containing not more than about 15 g/l of gypsum fines which enter the process.

Claim 11

The process of claim 1 wherein said sludging is conducted at about 10° to 45° C.

Claim 12

The process of claim 9 wherein said sludging is conducted at about 15° to 45° C.

Claim 13

The process of claim 11 wherein said sludging is conducted at about 15° to 21° C.

Claim 14

A flow process for the treatment of an aqueous ferrous sulfate waste stream from a sulfate process for producing titanium dioxide, the sulfuric acid in said stream having been at least partially neutralized with calcium carbonate and the resulting gypsum separated therefrom, which comprises: continuously passing said at least partially neutralized stream containing not more than about 15 g/l of gypsum fines, a recycled flow of coarser sludge solids from a later stage of the process, impalpable calcium carbonate selected from the group consisting of limestone, aragonite, oyster shell or mixtures thereof in about 1.03 to 1.4 times the stoichiometric amount, and air in about 10 to 100 times the stoichiometric amount into a series of atmospheric pressure, turbulently agitated reaction zones communicating serially with each other and therein substantially neutralizing any residual sulfuric acid and virtually completely sludging at a temperature of at least about 10° C. the iron content of said at least partially neutralized stream, continuously classifying the resulting sludge into a coarser solids fraction of which at least 10% by weight have average particle size of greater than 44 microns and an aqueous suspension of finer sludge solids; recycling between about 10% and 70% on a dry weight basis of said coarser sludge solids to the sludging operation; continuously separating said finer sludge solids from said aqueous suspension thereof; disposing as effluent the remainder of said aqueous suspension; and recovering the unrecycled portion of coarser sludge solids fraction.

Claim 15

A flow process for the treatment of an aqueous ferrous sulfate waste stream from a sulfate process for producing titanium dioxide, the sulfuric acid in said stream having been at least partially neutralized with calcium carbonate and the resulting gypsum separated therefrom, which comprises: continuously passing said at least partially neutralized stream containing not more than about 15 g/l of gypsum fines, a recycled flow of coarser sludge solids from a later stage of the process, impalpable calcium carbonate selected from the group consisting of limestone, aragonite, oyster shell or mixtures thereof in about 1.03 to 1.4 times the stoichiometric amount, and air in about 10 to 100 times the stoichiometric amount into a series of atmospheric pressure, turbulently agitated reaction zones communicating serially with each other and therein substantially neutralizing any residual sulfuric acid and virtually completely sludging at a temperature of at least about 10° C. the iron content of said at least partially neutralized stream, continuously classifying the resulting sludge into a coarser solids fraction of which at least 10% by weight have average particle size of greater than 44 microns and an aqueous suspension of finer sludge solids; recycling between about 10% and 70% on a dry weight basis of said coarser sludge solids to the sludging operation; continuously separating said finer sludge solids from said aqueous suspension thereof; disposing as effluent the remainder of said aqueous suspension; and recovering the unrecycled portion of coarser sludge solids fraction.