초록 ▼

The dust produced in the chlorination of titaniferous ores comprises essentially particulate ferrous chloride plus solid contaminants including coke and various metal chlorides and oxides and is oxidized in successive stages at relatively low temperatures to recover particulate iron oxide and gaseou

The dust produced in the chlorination of titaniferous ores comprises essentially particulate ferrous chloride plus solid contaminants including coke and various metal chlorides and oxides and is oxidized in successive stages at relatively low temperatures to recover particulate iron oxide and gaseous chlorine.

대표청구항 ▼

1. A multistage process for recovering gaseous chlorine and solid ferric oxide from chlorinator dust, said dust produced in the chlorination of titaniferous ores and comprising particulate ferrous chloride plus contaminates, said process comprising the steps of: (a) reacting said chlorinator dust at

1. A multistage process for recovering gaseous chlorine and solid ferric oxide from chlorinator dust, said dust produced in the chlorination of titaniferous ores and comprising particulate ferrous chloride plus contaminates, said process comprising the steps of: (a) reacting said chlorinator dust at temperatures of from 500° to 800° C. with oxygen in an amount sufficient only to form solid materials consisting essentially of particulate ferric oxide and gases consisting essentially of varporous ferric chloride; (b) separating the solid materials including the particulate ferric oxide from the gases produced in step a while maintaining the temperature in the range from 500° to 800° C.; (c) reacting the vaporous ferric chloride produced in step a with additional oxygen to form particulate ferric oxide and gases consisting essentially of gaseous chloride, the reaction in stage c being initiated at temperature from 600 ° to 800° C. followed by gradual lowering of the temperature to below 600° C.; and then (d) separating the particulate ferric oxide from the gases produced in stage c. 2. Multistage process for recovering gaseous chloride and solid ferric oxide from chlorinator dust according to claim 1 wherein the gases recovered in stage b include carbon dioxide. 3. Multistage process for recovering gaseous chlorine and solid ferric oxide from chlorinator dust according to claim 1 wherein the gases formed in stage a include gaseous ferric chloride and carbon dioxide. f 4. Multistage process for recovering gaseous chlorine and solid ferric oxide from chlorinator dust according to claim 1 wherein the temperature in stage c is lowered from between 600 and 800° C. to about 350° C. 5. Multistage process for recovering gaseous chlorine and solid ferric oxides from chlorinator dust according to claim 1 wherein elevated pressures are employed. 6. Multistage process for recovering gaseous chlorine and solid ferric oxides from chlorinator dust according to claim 1 wherein the gases formed in stage c are recycled to the chlorinator. 7. Multistage process for recovering gaseous chlorine and solid ferric oxide from chlorinator dust according to claim 1 wherein the solid materials produced in stage a includes both particulate ferric oxide and coke, reacting said solid materials with excess oxygen at temperatures above the ignition temperature of the coke to form a preheated mixture of gaseous oxygen and CO 2, separating the preheated gases from the solid material and recycling the preheated gases to stage a.