Granted Patent B2

US 7,943,103 · App. 11/412,816 · Granted May 17, 2011

Abstract

Claims (19)

1. A process for handling waste solids produced from the chlorination of titanium-bearing ores in the presence of coke as a reducing agent, comprising:

cooling a product stream from said chlorination of titanium-bearing ores which includes waste metal chloride solids and unreacted ore and coke solids;

separating waste metal chloride solids and unreacted ore and coke solids from gaseous components of the product stream;

combining the waste metal chloride solids and unreacted ore and coke solids with a liquid whereby waste metal chloride solids are dissolved in the liquid and unreacted ore and coke solids are slurried in the liquid;

separating out unreacted ore and coke solids from the liquid including the dissolved waste metal chlorides;

after separating out unreacted ore and coke solids from the liquid, dividing the liquid including the dissolved waste metal chlorides into a recycle substream or portion and a bleed substream or portion, the recycle substream or a portion of the recycle substream and the bleed substream or a portion of the bleed substream having a specific gravity of at least about 1.07;

recycling the recycle substream or portion to comprise at least a part of the liquid which is combined with the waste metal chloride solids and unreacted ore and coke solids in the product stream; and

neutralizing the bleed substream or portion to produce a filterable mass of waste metal hydroxide solids.

2. A process as defined in claim 1 , further comprising filtering the filterable mass of waste metal hydroxide solids to produce a landfillable waste metal hydroxide solids mass.

3. A process as defined in claim 1 , wherein the filterable mass of waste metal hydroxide solids is characterized by a solids content high enough to allow the filterable mass of waste metal hydroxide solids to be direct landfilled without being filtered.

4. A process as defined in claim 3 , wherein the solids content of the filterable mass is at least 45 percent by weight.

5. A process as defined in claim 1 , wherein the recycle substream or portion is characterized by a specific gravity of about 1.28 at about 20 degrees Celsius.

6. A process as defined in claim 1 , wherein the dissolved waste metal chlorides are neutralized by mixing with one or more solids including dry lime.

7. A process as defined in claim 6 , wherein the dissolved waste metal chlorides are neutralized by mixing first with one or more of cement kiln dust, lime kiln dust or fly ash, then mixing in dry lime.

8. A process as defined in claim 6 , wherein the dissolved waste metal chlorides are neutralized in one step with mixing of the dry lime and with fly ash.

9. A process as defined in claim 1 , wherein the waste metal chloride solids and unreacted ore and coke solids are separated from gaseous components of the product stream in a cyclone separator.

10. A process as defined in claim 9 , wherein the step of separating out unreacted ore and coke solids from the liquid including the dissolved waste metal chlorides employs at least a hydrocyclone.

11. A process as defined in claim 10 , wherein the unreacted ore and coke solids separated out at least in part by means of a hydrocyclone are recycled back to the chlorination step.

12. A process as defined in claim 3 , further comprising the step of disposing the filterable mass of waste metal hydroxide solids produced by the neutralization step in a landfill without first filtering the filterable mass of waste metal hydroxide solids.

Assignments (15)