Method for purification of gases

Claim 1

A method for selective purification of high temperature exhaust gas from a boiler plant comprising: (a) feeding an exhaust gas from a boiler plant containing excess oxygen, fly ash, and gaseous sulfur oxides to an electrostatic precipitator constructed and arranged to separate about 90 percent by weight of said fly ash; then, (b) first electrostatically percipitating about 90 percent by weight of said fly ash having a quality suitable for use in cement and oxidizing sulphur dioxide and sulphur trioxide by the corona discharge of the precipitator; (c) feeding the partially purified gas to another separator; then, (d) spraying the exhaust gas with an aqueous solution of calcium hydroxide absorption agent, to subsequently react with said gaseous sulphur oxides, in a concentration permitting a substantially dry product to be recovered using heat from the exhaust gas; then, (e) feeding the further partially-purified gas to a bag filter; and, (f) filtering the remaining fly ash with reacted absorption agent; whereby an exhaust gas, substantially free of fly ash and gaseous sulphur oxides; and fly ash, having a quality suitable for use in cement are recovered.

Claim 2

A method for selective purification of high temperature exhaust gas from a boiler plant comprising: (a) feeding an exhaust gas from a boiler plant containing excess oxygen, fly ash, and gaseous sulfur oxides to an electrostatic precipitator constructed and arranged to separate about 90 percent by weight of said fly ash; then, (b) first electrostatically percipitating about 90 percent by weight of said fly ash having a quality suitable for use in cement and oxidizing sulphur dioxide and sulphur trioxide by the corona discharge of the precipitator; (c) feeding the partially purified gas to another separator; then, (d) spraying the exhaust gas with an aqueous solution of calcium hydroxide absorption agent, to subsequently react with said gaseous sulphur oxides, in a concentration permitting a substantially dry product to be recovered using heat from the exhaust gas; then, (e) feeding the further partially-purified gas to a bag filter; and, (f) filtering the remaining fly ash with reacted absorption agent; whereby an exhaust gas, substantially free of fly ash and gaseous sulphur oxides; and fly ash, having a quality suitable for use in cement are recovered.

Claim 3

A method for selective purification of high temperature exhaust gas from a boiler plant comprising: (a) feeding an exhaust gas from a boiler plant containing excess oxygen, fly ash, and gaseous sulphur oxides to an electro static precipitator constructed and arranged to separate about 90 percent by weight of said fly ash; then, (b) first electrostatically precipitating about 90 percent by weight of said fly ash having a quality suitable for use in cement and oxidizing sulphur dioxide and sulphur trioxide by the corona discharge of the precipitator; (c) feeding the partially purified gas to another separator; then, (d) spraying the exhaust gas with an aqueous solution of calcium hydroxide absorption agent, to subsequently react with said gaseous sulphur oxides, in a concentration permitting a substantially dry product to be recovered using heat from the exhaust gas; then, (e) feeding the further partially-purified gas to an electrostatic precipitator; and, (f) filtering the remaining fly ash with reacted absorption agent; whereby an exhaust gas, substantially free of fly ash and gaseous sulphur oxides, and fly ash, having a quality suitable for use in cement, are recovered.

Claim 4

A method for selective purification of high temperature exhaust gas from a boiler plant comprising: (a) feeding an exhaust gas from a boiler plant containing excess oxygen, fly ash, and gaseous sulphur oxides to an electro static precipitator constructed and arranged to separate about 90 percent by weight of said fly ash; then, (b) first electrostatically precipitating about 90 percent by weight of said fly ash having a quality suitable for use in cement and oxidizing sulphur dioxide and sulphur trioxide by the corona discharge of the precipitator; (c) feeding the partially purified gas to another separator; then, (d) spraying the exhaust gas with an aqueous solution of calcium hydroxide absorption agent, to subsequently react with said gaseous sulphur oxides, in a concentration permitting a substantially dry product to be recovered using heat from the exhaust gas; then, (e) feeding the further partially-purified gas to an electrostatic precipitator; and, (f) filtering the remaining fly ash with reacted absorption agent; whereby an exhaust gas, substantially free of fly ash and gaseous sulphur oxides, and fly ash, having a quality suitable for use in cement, are recovered.