초록 ▼

In a cyclic adsorptive gas purification process, an impurity laden adsorbent is regenerated by exposing it first to an unheated gas for a pre-determined time period to desorb at least some of the impurity, followed by heating the adsorbent using a flowing stream of a heated gas to desorb the remaini

In a cyclic adsorptive gas purification process, an impurity laden adsorbent is regenerated by exposing it first to an unheated gas for a pre-determined time period to desorb at least some of the impurity, followed by heating the adsorbent using a flowing stream of a heated gas to desorb the remaining impurities over another pre-determined time period, further followed by cooling of the adsorbent using a flowing stream of gas for yet another pre-determined time period to make it ready for repeating the adsorptive cycle. Introducing an unheated purge stream reduces the energy requirements for the regeneration step compared to a traditional TSA process.

대표청구항 ▼

1. An energy efficient adsorbent regeneration process for the purification of feed air to a cryogenic distillation system in an air separation plant, said process comprising: feeding pressurized air for a first pre-determined time period to an adsorber operating at a first pressure to adsorb impurit

1. An energy efficient adsorbent regeneration process for the purification of feed air to a cryogenic distillation system in an air separation plant, said process comprising: feeding pressurized air for a first pre-determined time period to an adsorber operating at a first pressure to adsorb impurities in feed air onto one or more adsorbents within the adsorber;stopping pressurized air flow to the adsorber and depressurizing the adsorber to a second pressure that is lower than the first pressure;regenerating one or more adsorbents in a first regeneration step by flowing unheated regeneration gas through the adsorber operating at the second pressure for a second pre-determined time period effective to desorb a portion of the adsorbed impurities due to the lower adsorptive capacity of the adsorbent at the lower operating pressure of the unheated desorption step;further regenerating one or more adsorbents in a second regeneration step by flowing heated regeneration gas through the adsorber operating at the second pressure for a third pre-determined time period;cooling the one or more adsorbents by flowing adsorbent cooling gas through the adsorber at the second pressure for a fourth pre-determined time period;stopping the flow of adsorbent cooling gas and repressurizing the adsorber to the first pressure to begin feeding pressurized air. 2. The process of claim 1 wherein the adsorption pressure is from about 30 to about 600 psia. 3. The process of claim 1 wherein the temperature of the unheated regeneration gas of said first regeneration step is within about 20° F. of ambient temperature. 4. The process of claim 1 wherein the regeneration pressure in said first regeneration step is in the range of about 1 psi to about 5 psi above ambient pressure. 5. The process of claim 1 wherein the unheated regeneration gas comprises nitrogen. 6. The process of claim 1 wherein the said first regeneration step is conducted for a period of time in the range of about 5% to about 30% of the first pre-determined time period. 7. The process of claim 1 wherein the temperature of the heated regeneration gas of said second regeneration step is in the range of from about 300° F. to about 500° F. 8. The process of claim 1 wherein the regeneration pressure in said second regeneration step is in the range of about 1 psi to about 5 psi above ambient pressure. 9. The process of claim 1 wherein the heated regeneration gas comprises nitrogen. 10. The process of claim 1 wherein the said second regeneration step is conducted for a period of time in the range of about 10% to about 40% of the first pre-determined time period. 11. The process of claim 1 wherein the process is a cyclic thermal swing adsorption process. 12. The process of claim 1 wherein the adsorber contains at least two adsorbents. 13. The process of claim 12 wherein one of the adsorbent comprises activated alumina particles and the other adsorbent comprises molecular sieve adsorbent. 14. The process of claim 1 wherein the said first regeneration step is conducted for a period of time in the range of about 10% to about 30% of the first pre-determined time period. 15. The process of claim 1 wherein the said first regeneration step is conducted for a period of time in the range of about 15% to about 25% of the first pre-determined time period. 16. The process of claim 1 wherein the said second regeneration step is conducted for a period of time in the range of about 15% to about 30% of the first pre-determined time period. 17. The process of claim 1 wherein the impurities partially desorbed in said first regeneration step include CO2 and water.