IP Library Patent Application 16865569
Patent Application
App. No. 16/865,569

AMMONIA REMOVAL MATERIAL, AMMONIA REMOVAL METHOD, AND METHOD FOR MANUFACTURING HYDROGEN GAS FOR FUEL CELL AUTOMOBILE

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Patent No.
US None
App. No.
16/865,569
Abstract

An ammonia removal material to be used for obtaining a mixed gas (B) having an ammonia concentration of 0.1 mol ppm or less from a mixed gas (A) including hydrogen, nitrogen, and ammonia and having an ammonia concentration exceeding 0.1 mol ppm, the ammonia removal material containing zeolite having a pore size of 0.5 nm or more and 2.0 nm or less, a method for removing ammonia from the mixed gas using the ammonia removal material, and a method for producing a hydrogen gas for a fuel cell automobile, the method including the method for removing ammonia.

Claims (10)

1 . An ammonia removal method that removes ammonia so as to obtain a mixed gas (B) having an ammonia concentration of 0.1 mol ppm or less from a mixed gas (A) comprising hydrogen, nitrogen, and ammonia and having an ammonia concentration exceeding 0.1 mol ppm, the ammonia removal method comprising:

contacting the mixed gas (A) comprising hydrogen, nitrogen, and ammonia and having an ammonia concentration exceeding 0.1 mol ppm with an ammonia removal material comprising zeolite having a pore size of 0.5 nm or more and 2.0 nm or less.

2 . The ammonia removal method according to claim 1 , wherein the mixed gas (A) is derived from a decomposition gas obtained by decomposing ammonia at a decomposition temperature of 450° C. or higher and 600° C. or lower.

3 . The ammonia removal method according to claim 1 , wherein a crystal structure of the zeolite is at least one selected from the group consisting of an LTA type, an FAU type, a BEA type, an LTL type, an MFI type, an MWW type, an FER type, and an MOR type as a structural code.

4 . The ammonia removal method according to claim 1 , wherein a crystal structure of the zeolite is at least one selected from the group consisting of an A type, an X type, a β type, a Y type, an L type, a ZSM-5 type, an MCM-22 type, a ferrierite type, and a mordenite type.

5 . The ammonia removal method according to claim 1 , wherein the zeolite comprises as a cation at least one selected from a hydrogen ion, a lithium ion, a calcium ion, a sodium ion, a potassium ion, a magnesium ion, and a barium ion.

6 . The ammonia removal method according to claim 1 , wherein an ammonia content of the mixed gas (A) is 2,000 mol ppm or less.

7 . The ammonia removal method according to claim 1 , wherein the temperature for the contacting is 30° C. or lower.

8 . The ammonia removal method according to claim 1 , wherein the mixed gas (A) is obtained by decomposing ammonia by an ammonia decomposition method other than an autothermal system.

9 . The ammonia removal method according to claim 1 , wherein a H 2 O content of the mixed gas (A) is 5.0 mol % or less.

Assignments (1)
CHANGE OF NAME Recorded Jun 23, 2023
From: SHOWA DENKO K.K.
To: RESONAC CORPORATION
Reel/Frame 064082/0513 →