초록 ▼

A high capacity adsorbent may be used for enriching oxygen concentration in an air stream. Such a high capacity adsorbent may be from about 2 to about 3 times lighter relative to the currently available technology. Furthermore, the high capacity adsorbent is readily capable of regeneration after dea

A high capacity adsorbent may be used for enriching oxygen concentration in an air stream. Such a high capacity adsorbent may be from about 2 to about 3 times lighter relative to the currently available technology. Furthermore, the high capacity adsorbent is readily capable of regeneration after deactivation by water vapor. Unlike current available immobilization technology in which clay binder was used to bind 13X zeolite and additional 10% organic binder was used to immobilize beads, the adsorbents of the present invention may be made using just an organic binder, thereby reducing pore spoilage caused by the clay binder. Further unlike conventional adsorbents, which may use sodium as its cation, the adsorbent of the present invention uses a lithium cation, thereby resulting in enhanced nitrogen adsorption performance.

대표청구항 ▼

We claim: 1. A method for making an ion exchange adsorbent, the method comprising: binding the adsorbent with an organic polymer to form a bound adsorbent; calcining the bound adsorbent by thermal treatment at a temperature in the range of 150° C. to 400° C. to yield a calcined adsorbent; treating

We claim: 1. A method for making an ion exchange adsorbent, the method comprising: binding the adsorbent with an organic polymer to form a bound adsorbent; calcining the bound adsorbent by thermal treatment at a temperature in the range of 150° C. to 400° C. to yield a calcined adsorbent; treating the calcined adsorbent with a lithium salt to yield a treated adsorbent; washing the treated adsorbent with an aqueous base to yield a washed adsorbent; air drying the washed adsorbent to yield an air-dried adsorbent; drying the air-dried adsorbent in a vacuum to yield a vacuum-dried adsorbent; flowing preheated nitrogen through the vacuum-dried adsorbent, the temperature of the preheated nitrogen being about 300° C.; and immobilizing the adsorbent. 2. The method according to claim 1, further comprising packing the vacuum-dried adsorbent into a bed prior to flowing preheated nitrogen therethrough. 3. The method according to claim 1, wherein the adsorbent is zeolite 13X. 4. The method according to claim 1, wherein the temperature of the calcined adsorbent is controlled between about 50 to about 100° C. 5. The method according to claim 1, wherein the lithium salt is lithium chloride at a concentration from about 0.5 to about 5M. 6. The method according to claim 1, wherein the treated adsorbent is washed with aqueous sodium hydroxide having a pH of about 9. 7. The method according to claim 1, wherein the air-dried adsorbent is vacuum-dried at a temperature from about 50 to about 200° C. for a period from about 15 minutes to about 10 hours. 8. A method for making an ion exchange adsorbent, the method comprising: binding the adsorbent with a binder comprising an organic polymer and a cross-linked agent to form a bound adsorbent, the binder having a selected glassy temperature; calcining the bound adsorbent by thermal treatment, at a temperature in the range of 150° C., to 400° C., to yield a calcined adsorbent; treating the calcined adsorbent with a lithium salt to yield a treated adsorbent; washing the treated adsorbent with an aqueous base to yield a washed adsorbent; air drying the washed adsorbent to yield an air-dried adsorbent; drying the air-dried adsorbent in a vacuum to yield a vacuum-dried adsorbent; and flowing preheated nitrogen through the vacuum-dried adsorbent, the preheated nitrogen having a temperature of about 300° C. 9. A method for making an ion exchange adsorbent, the method comprising: binding the adsorbent with a binder comprising an organic polymer and a cross-linked agent to form a bound adsorbent; calcining the bound adsorbent by thermal treatment to yield a calcined adsorbent; treating the calcined adsorbent with a lithium salt to yield a treated adsorbent; washing the treated adsorbent with an aqueous base to yield a washed adsorbent; air drying the washed adsorbent to yield an air-dried adsorbent; drying the air-dried adsorbent in a vacuum to yield a vacuum-dried adsorbent; and flowing preheated nitrogen through the vacuum-dried adsorbent, the preheated nitrogen having a temperature of about 300° C.; wherein the adsorbent is zeolite 13X; and wherein the lithium salt is lithium chloride.