Zeolite y

Abstract

Process for preparing a modified zeolite Y which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from 700 to 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from 800 to 850° C. , (iii) the steam partial pressure is at least 0.03 bar at a temperature of from 850 to 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from 900 to 950° C. and (v) the steam partial pressure is at least 0.07 bar at a temperature of from 950 to 1000° C., a modified zeolite Y obtainable by such process, zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which has a peak at 3700 cm −1 but substantially no peaks at 3605 and 3670 cm −1 and zeolite Y having a silica to alumina molar ratio of at least 10, which zeolite Y has an acidity as measured by exchange with perdeuterated benzene of at most 20 micromole/gram.

1 . A process for preparing a modified zeolite Y which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from 700 to 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from 800 to 850° C. , (iii) the steam partial pressure is at least 0.03 bar at a temperature of from 850 to 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from 900 to 950° C. and (v) the steam partial pressure is at least 0.07 bar at a temperature of from 950 to 1000° C. 
     
     
         2 . A process according to  claim 1 , in which process the zeolite Y has a silica to alumina molar ratio of more than 10. 
     
     
         3 . A process according to  claim 2 , in which process the calcination is carried out during a time of from 20 minutes to 5 hours. 
     
     
         4 . A process according to  claim 3 , in which process the zeolite Y before calcination has a bulk silica to alumina molar ratio of greater than 13, a unit cell size in the range of from 24.10 to 24.40 Å, and a surface area of at least 875 m 2 /g. 
     
     
         5 . A modified zeolite Y prepared by subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from 700 to 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from 800 to 850° C. , (iii) the steam partial pressure is at least 0.03 bar at a temperature of from 850 to 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from 900 to 950° C. and (v) the steam partial pressure is at least 0.07 bar at a temperature of from 950 to 1000° C. 
     
     
         6 . The modified zeolite Y of  claim 5  wherein the zeolite Y has a silica to alumina molar ratio of more than 10. 
     
     
         7 . The modified zeolite Y of  claim 6 , wherein the calcination of the zeolite Y is carried out during a time of from 20 minutes to 5 hours. 
     
     
         8 . The modified zeolite Y of  claim 7 , wherein the zeolite Y before calcination has a bulk silica to alumina molar ratio of greater than 13, a unit cell size in the range of from 24.10 to 24.40 A, and a surface area of at least 875 m 2 /g. 
     
     
         9 . A zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which has a peak at 3700 cm −1  but substantially no peak at 3670 cm −1 . 
     
     
         10 . A zeolite Y having a silica to alumina molar ratio of at least 10, which zeolite Y has an acidity as measured by exchange with perdeuterated benzene of at most 20 micromole/gram. 
     
     
         11 . The zeolite Y according to  claim 10 , which zeolite Y has an acidity as measured by exchange with perdeuterated benzene of at most 10 micromole/gram. 
     
     
         12 . A method of using a zeolite, wherein a modified zeolite Y prepared by subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from 700 to 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from 800 to 850° C. , (iii) the steam partial pressure is at least 0.03 bar at a temperature of from 850 to 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from 900 to 950° C. and (v) the steam partial pressure is at least 0.07 bar at a temperature of from 950 to 1000° C. is used as an adsorbent. 
     
     
         13 . The modified zeolite Y of  claim 12  wherein the zeolite Y has a silica to alumina molar ratio of more than 10. 
     
     
         14 . The modified zeolite Y of  claim 13 , wherein the calcination of the zeolite Y is carried out during a time of from 20 minutes to 5 hours. 
     
     
         15 . The modified zeolite Y of  claim 14 , wherein the zeolite Y before calcination has a bulk silica to alumina molar ratio of greater than 13, a unit cell size in the range of from 24.10 to 24.40 A, and a surface area of at least 875 m 2 /g. 
     
     
         16 . A method of using a zeolite, wherein a modified zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which has a peak at 3700 cm −1  but substantially no peak at 3670 cm −1  is used as an adsorbent. 
     
     
         17 . A method of using a zeolite, wherein a modified zeolite Y having a silica to alumina molar ratio of at least 10, which zeolite Y has an acidity as measured by exchange with perdeuterated benzene of at most 20 micromole/gram is used as an adsorbent.