Alkali-promoted activated alumina adsorbent
An adsorbent for removing CO 2 from a gas mixture, the adsorbent comprising alumina and a carbonate compound where the carbonate to alumina IR absorbance intensity ratio is reduced by washing the adsorbent with water. The disclosure also describes a method of making adsorbent particles, process for removing CO 2 from a gas mixture using the adsorbent, and an adsorption unit using the adsorbent.
1. A method for making adsorbent particles for adsorbing CO 2 , the adsorbent particles comprising alumina, one or more alkali metals, and a carbonate compound, the method comprising:
washing alkali-promoted activated alumina materials comprising a carbonate compound with water; and
drying the washed alumina materials to form the adsorbent particles;
wherein the washed and dried adsorbent particles have a carbonate to alumina intensity ratio, R 2 , which is smaller than the carbonate to alumina intensity ratio, R 1 , of the alkali-promoted activated alumina materials before washing;
wherein the carbonate to alumina intensity ratio is as determined by Fourier Transform infrared spectroscopy of a crushed sample of the respective washed and dried adsorbent particles and a crushed sample of the alkali-promoted activated alumina materials before washing, wherein the carbonate to alumina intensity ratio is a ratio of a peak absorbance intensity for carbonate, AI carbonate , to a peak absorbance intensity for alumina, AI alumina , (i.e. R=AI carbonate /AI alumina )) each absorbance intensity obtained after subtracting a baseline signal intensity, where the peak absorbance intensity for alumina, AI alumina , is observed at an FTIR wavenumber in a range from 420 cm −1 to 520 cm −1 , and the peak absorbance intensity for carbonate, AI carbonate , is observed at an FTIR wavenumber in a range from 1300 cm −1 to 1400 cm −1 .
2. The method according to claim 1 wherein the water is deionized water.
3. The method according to claim 1 wherein the alkali-promoted activated alumina materials are washed sufficiently to produce adsorbent particles having a carbonate to alumina intensity ratio, R 2 , having a value less than or equal to 0.0150.
4. The method according to claim 1 wherein the alkali-promoted activated alumina materials are washed with water until the alkali-promoted activated alumina materials have a pH in solution of 9.5 or less thereby forming washed alumina materials, the pH in solution as determined by measuring the pH of an equilibrated 2 liter solution of deionized water containing 100 g of the washed alumina materials.
5. Adsorbent particles for use in a process to remove CO 2 from a gas mixture containing CO 2 made in a method according to claim 1 .
6. An adsorption unit comprising a bed containing the adsorbent particles according to claim 5 .
7. A method for making adsorbent particles for adsorbing CO 2 , the adsorbent particles comprising alumina, one or more alkali metals, and a carbonate compound, the method comprising:
washing alkali-promoted activated alumina materials comprising a carbonate compound with water; and
drying the washed alumina materials to form the adsorbent particles;
wherein the alkali-promoted activated alumina materials are washed sufficiently to produce adsorbent particles having a carbonate to alumina intensity ratio, R, the carbonate to alumina intensity ratio, R, having a value less than or equal to 0.0150, where the carbonate to alumina intensity ratio is as determined by Fourier Transform infrared spectroscopy of a crushed sample of the adsorbent particles, wherein the carbonate to alumina intensity ratio is a ratio of a peak absorbance intensity for carbonate, AI carbonate , to a peak absorbance intensity for alumina, AI alumina , (i.e. R=AI carbonate /AI alumina ), each peak absorbance intensity obtained after subtracting a baseline signal intensity, where the peak absorbance intensity for alumina, AI alumina , is observed at an FTIR wavenumber in a range from 420 cm −1 to 520 cm −1 , and the peak absorbance intensity for carbonate, AI carbonate , is observed at an FTIR wavenumber in a range from 1300 cm −1 to 1400 cm −1 .
8. Adsorbent particles for use in a process to remove CO 2 from a gas mixture containing CO 2 made in a method according to claim 7 .