Ruthenium-based catalyst for ammonia synthesis and preparation method and use thereof
Disclosed is a ruthenium-based catalyst for ammonia synthesis, preparation method and use thereof. The ruthenium-based catalyst comprises Ru—Ba-A core-shell structure which comprises a ruthenium nanoparticle as a core covered with a first shell and a second shell sequentially, wherein the first shell consists of a barium nanoparticle, and the second shell consists of a metal oxide. The Ru—Ba-A core-shell structure can effectively preventing agglomerations of ruthenium nanoparticles during the use of the catalyst and avoiding direct contact between the ruthenium nanoparticles and the metal oxides. In addition, barium nanoparticles have a promoting effect as an electronic promoter, which can effectively improve the stability and catalytic activity of ruthenium-based catalyst for ammonia synthesis, especially in the system for synthesizing ammonia from a coal gas.
1. A ruthenium-based catalyst for ammonia synthesis, comprising Ru—Ba-A core-shell structure, the Ru—Ba-A core-shell structure comprising a ruthenium nanoparticle as a core which is covered with a first shell and a second shell sequentially, wherein the first shell consists of a barium nanoparticle, and the second shell consists of a metal oxide;
wherein the support member is a graphitized activated carbon support; and the electron promoter is an oxide of an alkali metal;
the ruthenium-based catalyst is Ru—Ba-A-L/GC, wherein Ru represents a ruthenium nanoparticle, Ba represents a barium nanoparticle, A represents a metal oxide, L represents an electron promoter, GC represents a graphitized activated carbon support, and L/GC represents a composite support;
the metal oxide is barium oxide or a mixture of barium oxide and oxide MO X , wherein M is a metal except for barium, and X is 1-2;
the oxide MO X is at least one selected from the group consisting of ZrO 2 , TiO 2 , MgO, ZnO, CeO 2 , Al 2 O 3 , La 2 O 3 and Sm 2 O 3 .
2. The ruthenium-based catalyst of claim 1 , further comprising a composite support which comprises a support member having an electron promoter dispersed on a surface of the support member, and the Ru—Ba-A core-shell structure being supported on the composite support.
3. The ruthenium-based catalyst of claim 2 , wherein based on mass of the support member, the ruthenium nanoparticle accounts for 3 wt. % to 5 wt. %, metal ions in the barium nanoparticle and metal oxide account for 3 wt. % to 20 wt. %, and metal ions in the electron promoter account for 3 wt. % to 10 wt. %.
4. The ruthenium-based catalyst of claim 3 , wherein the electron promoter is K 2 O.
5. The ruthenium-based catalyst of claim 4 , wherein the core has an average diameter of 2 nm to 5 nm, and the first shell and second shell have a total average thickness of 1 nm to 2 nm; and wherein the graphitized activated carbon support has a specific surface area of 800 m 2 /g to 1500 m 2 /g and a pore volume of 0.4 cm 3 /g to 0.8 cm 3 /g.
6. A method for preparing the ruthenium based catalyst of claim 1 for ammonia synthesis, comprising the following steps:
impregnating a support member with a mixed aqueous solution of a ruthenium precursor, a soluble salt of a metal and a soluble salt of an electron promoter, and taking out the impregnated support member after the impregnating is completed; and
successively drying and calcinating the impregnated support member in a reducing atmosphere to obtain a ruthenium-based catalyst for ammonia synthesis.
7. The method of claim 6 , wherein the impregnating is incipient impregnation carried out at a temperature of 20° C. to 60° C.;
the drying is carried out at a temperature of 110° C. to 120° C.; and
the calcinating comprises heating the impregnated support member after drying from a temperature of 110° C. to 120° C. to a temperature of 500° C. to 900° C. at a heating rate of 2-10° C./h, and then calcinating at 500° C. to 900° C.
8. The method of claim 7 , wherein the calcinating lasts for 1 h to 60 h.
9. The method of claim 8 , wherein the reducing atmosphere is a coal gas atmosphere comprising CO and CO 2 at a concentration of 5 ppm to 20 ppm; and
the mixed aqueous solution has a pH value of 0-2.
10. The method of claim 8 , wherein every 100 g of the mixed aqueous solution contains 1-4 g ruthenium ions, and a mass ratio of the ruthenium ions to metal ions in the soluble salt of a metal oxide to metal ions in the soluble salt of the electron promoter is 1:(1.2 to 1):10.
11. The method of claim 7 , wherein the reducing atmosphere is a coal gas atmosphere comprising CO and CO 2 at a concentration of 5 ppm to 20 ppm; and
the mixed aqueous solution has a pH value of 0-2.
12. The method of claim 7 , wherein every 100 g of the mixed aqueous solution contains 1-4 g ruthenium ions, and a mass ratio of the ruthenium ions to metal ions in the soluble salt of a metal oxide to metal ions in the soluble salt of the electron promoter is 1:(1.2 to 1):10.
13. The method of claim 7 , wherein the method further comprises an aging step after the impregnating and prior to the drying, and the aging step is carried out at a temperature of 20° C. to 30° C. for a period of 2 h to 12 h.
14. The method of claim 12 , wherein the pH value of the mixed aqueous solution is adjusted with one or more acids selected from the group consisting of nitric acid, acetic acid, oxalic acid, citric acid and tartaric acid;
and/or, the ruthenium precursor is a chlorine-free water-soluble ruthenium precursor selected from the group consisting of ruthenium acetate, ruthenium nitrosyl nitrate, ruthenium ammonia complex and any combination thereof,
and/or, the soluble salt of the metal and the soluble salt of the electron promoter are both selected from the group consisting of nitrate, acetate, citrate, oxalate and any combination thereof.