Fe(II)-substituted beta type zeolite, gas adsorbent containing same and method for producing same, and method for removing nitrogen monoxide and hydrocarbon
To provide an Fe(II)-substituted beta type zeolite which has been ion-exchanged with Fe(II) ions and can effectively adsorb and remove nitrogen monoxide or hydrocarbon contained in gas to be cleaned, even if oxygen is present in the gas at a high concentration or the temperature of the gas is low. In the Fe(II)-substituted beta type zeolite, a ratio of SiO 2 /Al 2 O 3 is preferably 10 to 18, a BET specific surface area is preferably 400 m 2 /g to 700 m 2 /g, a micropore specific surface area is preferably 290 m 2 /g to 500 m 2 /g, and a micropore volume is preferably 0.15 cm 3 /g to 0.25 cm 3 /g. The amount of Fe(II) supported is preferably 0.01% by mass to 6.5% by mass based on the Fe(II)-substituted beta type zeolite.
1. An Fe(II)-substituted beta type zeolite which has been ion-exchanged with Fe(II) ions,
wherein a ratio of SiO 2 /Al 2 O 3 is 10 to 18, a BET specific surface area is 400 m 2 /g to 700 m 2 /g, a micropore specific surface area is 290 m 2 /g to 500 m 2 /g, and a micropore volume is 0.15 cm 3 /g to 0.25 cm 3 /g.
2. The Fe(II)-substituted beta type zeolite according to claim 1 ,
wherein the amount of Fe(II) supported is 0.01% by mass to 6.5% by mass based on the Fe(II)-substituted beta type zeolite.
3. The Fe(II)-substituted beta type zeolite according to claim 1 that uses, as a beta type zeolite which has not yet been ion-exchanged with Fe(II) ions, a beta type zeolite in which a ratio of SiO 2 /Al 2 O 3 is 10 to 16, a BET specific surface area that is measured in a state of a sodium-type is 500 m 2 /g to 700 m 2 /g, a micropore specific surface area is 350 m 2 /g to 500 m 2 /g, and a micropore volume is 0.15 cm 3 /g to 0.25 cm 3 /g.
4. The Fe(II)-substituted beta type zeolite according to claim 3 that uses, as a beta type zeolite of which has not yet been ion-exchanged with Fe(II) ions, a beta type zeolite which is obtained by
(1) mixing a silica source, an alumina source, and an alkali source with water to obtain a reaction mixture having a composition represented by the following molar ratio,
SiO 2 /Al 2 O 3 =40 to 200
Na 2 O/SiO 2 =0.22 to 0.4
H 2 O/SiO 2 =10 to 50
(2) using, as a seed crystal, a beta type zeolite which has a ratio of SiO 2 /Al 2 O 3 of 8 to 30 and does not contain an organic compound having an average particle size of 150 nm or larger, and adding the seed crystal to the reaction mixture in a proportion of 0.1% by mass to 20% by mass based on a silica component in the reaction mixture, and
(3) heating the reaction mixture, to which the seed crystal has been added, at 100° C. to 200° C. in a sealed state.
5. A gas adsorbent containing the Fe(II)-substituted beta type zeolite according to claim 1 .
6. The gas adsorbent according to claim 5 that is used for adsorbing nitrogen monoxide.
7. The gas adsorbent according to claim 5 that is used for adsorbing hydrocarbon.
8. A method for producing an Fe(II)-substituted beta type zeolite, comprising:
a step of causing Fe(II) ions to be supported on a beta type zeolite by dispersing the beta type zeolite, in which a ratio of SiO 2 /Al 2 O 3 is 10 to 16, a BET specific surface area that is measured in a state of sodium type is 500 m 2 /g to 700 m 2 /g, a micropore specific surface area is 350 m 2 /g to 500 m 2 /g, and a micropore volume is 0.15 cm 3 /g, to 0.25 cm 3 /g, in an aqueous solution of a water-soluble divalent iron compound, and performing mixing under stirring.
9. The production method according to claim 8 ,
wherein during the mixing under stirring, ascorbic acid of a mole number that is 0.1 to 3 times greater than that of the divalent iron is added to the aqueous solution.
10. A method for removing nitrogen monoxide and/or hydrocarbon, comprising:
causing the nitrogen monoxide to be adsorbed and/or the hydrocarbon to be adsorbed onto an Fe(II)-substituted beta type zeolite by bringing the nitrogen monoxide or nitrogen monoxide-containing gas and/or the hydrocarbon or hydrocarbon-containing gas into contact with the Fe(II)-substituted beta type zeolite which has been ion-exchanged with Fe(II) ions and in which a ratio of SiO 2 /Al 2 O 3 is 10 to 18, a BET specific surface area is 400 m 2 /g to 700 m 2 /g, a micropore specific surface area is 290 m 2 /g to 500 m 2 /g, and a micropore volume is 0.15 cm 3 /g to 0.25 cm 3 /g.