Gas purification process
A process for the purification of hydrogen based gas mixtures utilizing zeolite X wherein the particle size distribution of the zeolite X powder has a coefficient of variation from about 15% to about 30%.
1. A process for the separation and purification of hydrogen contained in a gas mixture contaminated by impurities which comprises contacting the gas mixture to be purified in an adsorption region containing an adsorbent comprising a zeolite X powder wherein the particle size distribution of the zeolite X powder has a coefficient of variation from about 15% to about 30%.
2. The process of claim 1 wherein the gas mixture to be purified contains more than about 50 percent of gaseous hydrogen.
3. The process of claim 1 wherein the adsorption region is maintained under a pressure from about 790 kPa (100 psig) to about 7000 kPa (1000 psig).
4. The process of claim 1 wherein the silica/alumina ratio of the zeolite X powder is between 2.0 and 2.5.
5. The process of claim 1 wherein the mean diameter of the zeolite X particles range from about 4 to about 12 microns.
6. The process of claim 1 wherein the mean diameter of the zeolite X particles range from 6 to 10 microns.
7. The process of claim 1 wherein a pressure swing adsorbent system is utilized.
8. A process for the separation and purification of hydrogen contained in a gas mixture contaminated by impurities which comprises contacting the gas mixture to be purified in an adsorption region containing an adsorbent comprising a zeolite X powder synthesized by providing a slurry of seed crystals at reaction conditions; adding to the slurry nutrients, to provide framework elements of the seed crystals thereby growing the seed crystals; performing the addition at a rate that essentially equals the crystal growth rate and for a time sufficient to produce the zeolite X powder.
9. The process of claim 8 wherein the gas mixture to be purified contains more than about 50 percent of gaseous hydrogen.
10. The process of claim 8 wherein the adsorption region is maintained under a pressure from about 790 kPa (100 psig) to about 7000 kPa (1000 psig).
11. The process of claim 8 wherein the silica/alumina ratio of the zeolite X powder is between 2.0 and 2.5.
12. The process of claim 8 wherein the mean diameter of the zeolite X powder particles range from about 4 to about 12 microns.
13. The process of claim 8 wherein the mean diameter of the zeolite X powder particles range from 6 to 10 microns.
14. The process of claim 8 wherein a pressure swing adsorbent system is utilized.
15. The process of claim 8 wherein the zeolite X powder has a particle size distribution has a coefficient of variation from about 15% to about 30%.
16. A process for the separation and purification of hydrogen contained in a gas mixture contaminated by impurities which comprises contacting the gas mixture to be purified in a pressure swing adsorbent system containing an adsorbent comprising a zeolite X powder wherein the particle size distribution of the zeolite X powder has a coefficient of variation from about 15% to about 30% and the mean diameter of the zeolite X powder particles range from about 6 to about 12 microns, and wherein the cycle time is less than about 4 minutes to achieve a hydrogen recovery of at least about 88 volume percent.
17. The process of claim 16 wherein the adsorbent has a bulk crush strength of greater than about 960 kPa (125 psig).
18. The process of claim 16 wherein the gas mixture to be purified contains more than about 50 percent of gaseous hydrogen.
19. The process of claim 16 wherein the silica/alumina ratio of the zeolite X powder is between 2.0 and 2.5.
20. A process for the separation and purification of hydrogen contained in a gas mixture contaminated by impurities which comprises:
(a) passing a hydrogen based gas mixture contaminated by at least carbon monoxide and containing at least one other impurity selected from the group consisting of carbon dioxide, nitrogen and C 1 -C 8 hydrocarbons into an adsorption region comprising at least one first adsorbent bed containing a first adsorbent selective for at least carbon dioxide and C 1 -C 8 hydrocarbons, and one second adsorbent bed composed of a second adsorbent bed composed of a second adsorbent comprising a zeolite X powder wherein the particle size distribution of the zeolite X powder has a coefficient of variation from about 15% to about 30%;
(b) desorbing the carbon monoxide and the other impurity or impurities adsorbed on the at least first and second adsorbents by inducing a pressure gradient and progressively lowering the pressure in the adsorption region, so as to desorb the carbon monoxide and the other impurity or impurities via an inlet to the adsorption region; and
(c) raising the pressure in the adsorption region.
21. The process of claim 20 wherein the gas mixture to be purified contains more than about 50 percent of gaseous hydrogen.
22. The process of claim 20 wherein the adsorption region is maintained under a pressure from about 790 kPa (100 psig) to about 7000 kPa (1000 psig).
23. The process of claim 20 wherein the silica/alumina ratio of the zeolite X powder is between 2.0 and 2.5.
24. The process of claim 20 wherein the mean diameter of the zeolite X powder particles range from about 4 to about 12 microns.