Zeolite Y
AssigneePQ Corporation
InventorsDavid Allen Cooper, Cornelius Ouwehand, Laszlo Domokos, Lay Hwa Ong
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AssigneePQ Corporation
InventorsDavid Allen Cooper, Cornelius Ouwehand, Laszlo Domokos, Lay Hwa Ong
Estimating the term…
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.
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° C. to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from greater than 700° C. to less than 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from greater than 800° C. to less than 850° C., (iii) the steam partial pressure is at least 0.03 bar at a temperature of from greater than 850° C. to less than 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from greater than 900° C. to less than 950° C. or (v) the steam partial pressure is at least 0.07 bar at a temperature of from greater than 950° C. to less than 1000° C.
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° C. to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from greater than 700° C. to less than 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from greater than 800° C. to less than 850° C., (iii) the steam partial pressure is at least 0.03 bar at a temperature of from greater than 850° C. to less than 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from greater than 900° C. to less than 950° C. or (v) the steam partial pressure is at least 0.07 bar at a temperature of from greater than 950° C. to less than 1000° C.
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.
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.
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° C. to 1000° C. wherein (i) the steam partial pressure is at most 0.06 bar at a temperature of from greater than 700° C. to less than 800° C., (ii) the steam partial pressure is at most 0.08 bar at a temperature of from greater than 800° C. to less than 850° C., (iii) the steam partial pressure is at least 0.03 bar at a temperature of from greater than 850° C. to less than 900° C., and (iv) the steam partial pressure is at least 0.05 bar at a temperature of from greater than 900° C. to less than 950° C. or (v) the steam partial pressure is at least 0.07 bar at a temperature of from greater than 950° C. to less than 1000° C. is used as an adsorbent.
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.
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.
Dependencies are inferred from the claim text.