초록 ▼

The invention relates to a method and system for purifying exhaust gas, especially a solvent-containing exhaust gas from refrigerator recycling, wherein the dried, pressurized exhaust gas is cryogenically condensed, the condensed components are separated from the remaining exhaust gas, the cold and

The invention relates to a method and system for purifying exhaust gas, especially a solvent-containing exhaust gas from refrigerator recycling, wherein the dried, pressurized exhaust gas is cryogenically condensed, the condensed components are separated from the remaining exhaust gas, the cold and purified pressurized exhaust gas is passed through an adsorber to adsorbe the remaining condensed components, the adsorber is purged with a warmed gas stream, namely either a warmed inert gas stream or the purified exhaust gas respectively at reduced pressure, and the desorbed gas is recycled.

대표청구항 ▼

What is claimed is: 1. A method for purifying solvent-containing gas comprising the steps of: a) cryogenically condensing a dewatered pressurized, solvent-containing gas to create condensed components and remaining gas; b) separating the condensed components from the remaining gas; c) passing the r

What is claimed is: 1. A method for purifying solvent-containing gas comprising the steps of: a) cryogenically condensing a dewatered pressurized, solvent-containing gas to create condensed components and remaining gas; b) separating the condensed components from the remaining gas; c) passing the remaining gas through an adsorber to absorbe condensed solvents that remain in said remaining gas; d) purging the adsorber with a warmed inert gas stream to desorb condensed solvents thereby creating a desorbed gas stream; and e) recycling the desorbed gas stream from said adsorber. 2. The method according to claim 1, wherein prior to said cryogenically condensing step, is a step of compressing the solvent-containing gas to a pressure between 2 and 25 bars. 3. The method according to claim 1, wherein the recycling step is accomplished by combining said desorbed gas stream with said solvent-containing gas prior to the cryogenically condensing step and repeating the steps a-e. 4. The method according to claim 1, characterized in that the adsorber in said passing step is operated under cryogenic conditions at a temperature of less than-20째 C. 5. The method according to claim 1, characterized in that the purging step is performed at atmospheric pressure. 6. The method according to claim 1, wherein the cryogenically condensing and passing steps are performed at pressures that are about the same. 7. The method according to claim 1, wherein prior to said cryogenically condensing step, are multiple steps of condensing the solvent-containing gas to create a dewatered solvent-containing gas. 8. The method according to claim 7, wherein produced ice hydrates are removed as particles during at least one of said multiple steps of condensing. 9. The method according to claim 1, wherein prior to said cryogenically condensing step, are multiple steps of condensing and at least one compressing step to create a dewatered, pressurized, solvent-containing gas. 10. The method according to claim 1 wherein said solvent-containing gas is an exhaust gas produced from the step of refrigerator recycling. 11. A system for purifying solvent-containing gas comprising: a) a compressor for compressing the gas; b) a separator for separating water and/or solvent from the compressed gas; c) a cryogenic condenser for condensing the dried, compressed gas; d) a separator for removing the condensed solvents from the remaining gas; and e) a pressure swing adsorber for adsorbing the remaining condensed solvents wherein the cryogenic condenser is cooled with a liquefied inert gas, and wherein evaporated liquefied inert gas from the cryogenic condenser is used for desorption of said adsorber. 12. The system according to claim 11, wherein a second pressure swing adsorber is disposed between said compressor and said cryogenic condenser. 13. The system according to claim 12, wherein at least one of the two adsorbers comprises at least two zeolithic molecular sieves connected in parallel. 14. The system according to claim 12, wherein a recuperator is disposed both between the second adsorber and the cryogenic condenser and between the cryogenic condenser and the first adsorber. 15. The system according to claim 14, wherein the cryogenic condenser is cooled with a liquefied inert gas, and wherein the evaporated nitrogen from the cryogenic condenser is used to cool the recuperator. 16. The system according to claim 14, wherein the cryogenic condenser is cooled with a liquefied inert gas, and wherein the evaporated nitrogen from the cryogenic condenser is used to desorb the second adsorber. 17. The system according to claim 15, wherein the cryogenic condenser is cooled with a liquefied inert gas, and wherein the evaporated nitrogen from the cryogenic condenser is used to desorb the second adsorber.