Ceramic base material, ceramic support, and separation membrane complex
US-2024399316-A1 · Dec 5, 2024 · US
US10207248B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10207248-B2 |
| Application number | US-201314358975-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 2, 2013 |
| Priority date | Apr 2, 2012 |
| Publication date | Feb 19, 2019 |
| Grant date | Feb 19, 2019 |
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A methyl iodide adsorber, comprising a zeolite containing at least one iodide-adsorbing metal or a compound thereof, wherein the zeolite is a hydrophobic zeolite. Also, a use of the adsorber and a method for the adsorption of methyl iodide.
Opening claim text (preview).
The invention claimed is: 1. An iodide or iodine adsorber, comprising a zeolite containing at least one iodide- or iodine-adsorbing metal or a compound thereof, wherein the zeolite is a hydrophobic zeolite having an SiO 2 /Al 2 O 3 ratio>30, and wherein the zeolite is BEA. 2. The adsorber according to claim 1 , in which the zeolite is an intrinsically hydrophobic zeolite. 3. The adsorber according to claim 1 , in which the zeolite is microporous. 4. The adsorber according to claim 1 , in which the zeolite or the adsorber has a proportion of micropores of more than 70%, relative to the total pore volume of the zeolite or of the adsorber. 5. The adsorber according to claim 1 , in which the zeolite is an aluminium silicate. 6. The adsorber according to claim 1 , in which at least one promoter is contained for reducing the water decomposition by the iodide-adsorbing metal. 7. The adsorber according to claim 6 , in which the promoter comprises lead. 8. The adsorber according to claim 1 , in which the zeolite or the adsorber has a BET surface area of 10 to 1000 m 2 /g. 9. The adsorber according to claim 1 , in which the adsorber is formed as bulk material. 10. The adsorber according to claim 9 , in which the adsorber is formed as extrudate, as shaped bodies or as particles coated with the zeolite. 11. A method for the adsorption of gaseous methyl iodide, gaseous radioactive methyl iodide, gaseous iodine and/or gaseous radioactive iodine, comprising contacting gaseous methyl iodide, gaseous radioactive methyl iodide, gaseous iodine and/or gaseous radioactive iodine with the adsorber of claim 1 . 12. The method according to claim 11 , in which the adsorber is used in or in the vicinity of nuclear power plants, reprocessing plants or fuel element storage facilities; and/or in which the adsorber is used together with a hydrogen recombination catalyst. 13. A process for the adsorption of gaseous methyl iodide, in which gaseous methyl iodide is brought into contact with an adsorber according to claim 1 . 14. A process according to claim 13 , in which the gaseous methyl iodide is radioactive; and/or in which gaseous iodine and/or gaseous radioactive iodine is additionally adsorbed by the adsorber. 15. The adsorber according to claim 1 , wherein the iodide or iodine is adsorbed from a gas phase onto said zeolite. 16. The adsorber according to claim 1 , wherein the zeolite has an SiO 2 /Al 2 O 3 ratio>50. 17. The adsorber according to claim 1 , wherein the iodide- or iodine-adsorbing metal is selected from silver, yttrium, cerium, magnesium, sodium, tin, and lead. 18. The adsorber according to claim 1 , wherein the iodide-adsorbing metal is situated in the pores of the zeolite. 19. The adsorber according to claim 1 , wherein the zeolite has an SiO 2 /Al 2 O 3 ratio>100. 20. The adsorber according to claim 6 , wherein the content of iodide- or iodine-adsorbing metal in the zeolite or in the adsorber is 0.1 to 50 wt. %. 21. The adsorber according to claim 6 , wherein the content of promoter in the zeolite or in the adsorber is 1 to 30 wt. %. 22. The adsorber according to claim 1 , wherein the integral pore volume of the zeolite or of the adsorber is greater than 100 mm 3 /g. 23. The adsorber according to claim 1 , wherein the adsorber comprises a support comprising the zeolite. 24. The adsorber according to claim 1 wherein the adsorber comprises a support wherein the support comprises a washcoat comprising the zeolite. 25. The adsorber according to claim 9 , wherein the adsorber is formed as extrudate, as shaped bodies, or as particles coated with the zeolite. 26. The adsorber according to claim 24 , wherein the adsorber is formed as extrudate, as shaped bodies or as particles coated with the zeolite. 27. The adsorber according to claim 9 wherein the adsorber is formed honey-combed-shaped or plate-shaped. 28. The adsorber according to claim 24 wherein the adsorber is formed honey-combed-shaped or plate-shaped. 29. The adsorber according to claim 9 wherein the support is formed honey-combed-shaped or plate-shaped. 30. The adsorber according to claim 24 wherein the support is formed honey-combed-shaped or plate-shaped. 31. An iodide or iodine adsorber, comprising a BEA zeolite comprising between 10% and 20% of at least one metal or compound thereof capable of methyl-iodide adsorption, wherein the metal or compound thereof is selected from the group consisting of silver, yttrium, cerium, magnesium, sodium, tin and lead; and wherein the BEA zeolite has a ratio of SiO 2 /Al 2 O 3 between 100 and 250, and is microporous. 32. The iodide or iodine adsorber according to claim 31 , wherein the metal or compound thereof is silver. 33. The iodide or iodine adsorber according to claim 31 , further comprising at least one promoter for reducing the water decomposition by the iodide-adsorbing metal, wherein the promotor comprises lead. 34. The iodide or iodine adsorber according to claim 31 , wherein a ratio of the at least one metal or compound thereof capable of methyl-iodide adsorption to the lead is from 6:1 to 1:1.
Honeycomb or cellular structures; Solid foams or sponges · CPC title
comprising inorganic material · CPC title
by measuring contact angle · CPC title
Pore volume, e.g. total pore volume, mesopore volume, micropore volume · CPC title
Surface area, e.g. BET-specific surface · CPC title
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