Ammonia synthesis catalyst and method for producing same

Patent metadata

Field	Value
Publication number	US-2018071719-A1
Application number	US-201615552203-A
Country	US
Kind code	A1
Filing date	Feb 19, 2016
Priority date	Feb 20, 2015
Publication date	Mar 15, 2018
Grant date	—

Abstract

The present invention provides a rare earth oxide-supported noble metal catalyst which has a high catalytic activity, is greatly improved in the ammonia production activity per weight of the catalyst and per amount of the supported metal, and enables the synthesis of ammonia under mild conditions. The catalyst according to the present invention is characterized in that ruthenium is supported in a layered form on a praseodymium oxide carrier. The catalyst according to the present invention can be produced by burning a praseodymium oxide precursor at a lower temperature, then at a medium temperature and then at a higher temperature to produce praseodymium oxide, then agitating the resultant praseodymium oxide together with a ruthenium supply source in a solvent, then removing the solvent from the mixture, and then burning the resultant product.

First claim

1 . An ammonia synthesis catalyst, characterized in that ruthenium is supported so as to be layered on a praseodymium oxide carrier.

2 . The ammonia synthesis catalyst according to claim 1 , characterized in that the amount of Ru supported is 1 to 10% by weight of the total amount of the Ru-supported catalyst.

3 . The ammonia synthesis catalyst according to claim 1 , characterized in that the Ru layer on the carrier has a thickness of larger than or equal to 0.1 nm.

4 . A method for producing an ammonia synthesis catalyst, characterized in that a praseodymium oxide precursor is converted to praseodymium oxide by firing the precursor at low, middle and high temperatures in this order, the converted praseodymium oxide is stirred together with a ruthenium source in a solvent, the solvent is removed from the mixture, and then the rest is fired, to thereby make ruthenium be supported so as to be layered on the praseodymium oxide carrier.

5 . The method for producing an ammonia synthesis catalyst according to claim 4 , characterized in that the praseodymium oxide precursor is fired at 200 to 400° C. for 1 to 10 hours, 400 to 600° C. for 1 to 10 hours and 600 to 900° C. for 1 to 10 hours in this order.

6 . The method for producing an ammonia synthesis catalyst according to claim 4 , characterized in that an organometal compound is used as the ruthenium source.

7 . The method for producing an ammonia synthesis catalyst according to claim 6 , characterized in that an organic solvent is used as the solvent.

8 . The method for producing an ammonia synthesis catalyst according to claim 4 or 5 , characterized in that triruthenium dodecacarbonyl is used as the ruthenium source, and tetrahydrofuran is used as the solvent.

9 . The ammonia synthesis catalyst according to claim 2 , characterized in that the Ru layer on the carrier has a thickness of larger than or equal to 0.1 nm.

10 . The method for producing an ammonia synthesis catalyst according to claim 5 , characterized in that an organometal compound is used as the ruthenium source.

11 . The method for producing an ammonia synthesis catalyst according to claim 10 , characterized in that an organic solvent is used as the solvent.

Assignees

• Japan Science & Tech Agency
• Japan Science & Tech Agency

Inventors

• Nagaoka Katsutoshi
• Imamura Kazuya
• Sato Katsutoshi

Classifications

• C01P2004/03

  obtained by SEM · CPC title

• B01J37/0225

  of metal substrates · CPC title

• B01J37/18

  with gases containing free hydrogen · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C01C1/0411

  characterised by the catalyst · CPC title