Shell impregnated catalyst and process for producing a shell impregnated catalyst body
A process for producing a catalyst, comprising the steps of modifying a carrier by a first impregnation with at least one alkaline earth metal in a first metal precursor solution, the first metal precursor being decomposed to form at least one metal oxide or metal hydroxide, thereby obtaining a modified carrier. A second impregnation is carried out by incipient wetness by a second precursor solution comprising at least one metal Me in a second solution. Finally, the second precursor is decomposed, thereby obtaining a catalyst body having an enrichment of the at least one metal Me in the outer shell of the catalyst body, the metal being present in a concentration having either as an egg-shell profile or a hammock profile.
1. A process for producing a catalyst body, said process comprising the steps of:
providing a carrier comprising magnesium alumina spinel and/or Calcium aluminates, wherein the carrier has a pore volume 200-400 ml/kg and a BET surface area 2-50 m 2 /g,
modifying said carrier by a first impregnation with at least one alkaline earth metal in a first metal precursor solution, wherein the alkaline earth metal is selected from the group consisting of Mg, Ca, and Ba,
decomposing the first metal precursor at a temperature of from 300-900° C. to form an alkaline earth metal oxide or alkaline earth metal hydroxide layer on the carrier, thereby obtaining a modified carrier,
carrying out a second impregnation by a second precursor solution comprising at least one metal Me in a second solution, the metal Me comprising a catalytic metal, wherein the second precursor solution is Me-nitrate, Me-citrate, Me-Ethylenediaminetetraacetic acid (EDTA), or Me-Ethylenediamine (EDA) and
decomposing the second precursor to metal oxide, thereby obtaining a catalyst body having an enrichment of the at least one catalytic metal Me in an outer shell of the catalyst body, said at least one catalytic metal Me being present in a concentration having either an egg-shell profile and/or a hammock profile.
2. A process according to claim 1 , wherein the first precursor solution is a nitrate, carbonate or hydroxide of the alkaline earth metals.
3. A process according to claim 1 , wherein the first decomposition is carried out at 350-550° C.
4. A process according to claim 1 , wherein the alkaline earth metal concentration in the carrier is 0.5-10 wt %, after impregnation.
5. A process according to claim 1 , wherein the catalytic metal Me is Ni, Ru, Rh, Ir, Pd and/or Pt.
6. A process according to claim 1 , wherein the catalytic metal Me is Ni, Ru and/or Rh.
7. A process according to claim 1 , wherein the impregnated carrier is dried between the second impregnation and the second decomposition.
8. A process according to claim 1 , wherein the second decomposition is carried out at 350-600° C.
9. A process according to claim 1 , wherein the alkaline earth metal oxide/hydroxide concentration is 1-6 wt % of the carrier.
10. A process according to claim 1 , wherein 90% of the catalytic metal Me present within an outer later having a thickness of up to 500 μm.
11. A process according to claim 1 , wherein the second impregnation is carried out by incipient wetness.
12. A process according to claim 1 , wherein the obtained catalyst body comprises a core section and the outer shell, wherein the core comprises carrier material impregnated with the alkali earth metal oxide or alkali earth metal hydroxide, wherein the outer shell comprises the carrier material impregnated with the alkali earth metal oxide or alkali earth metal hydroxide and the catalytic metal Me.
13. A process according to claim 1 , wherein the catalytic metal Me is Ni.
14. A process for producing a catalyst body, said process comprising the steps of:
providing a carrier comprising magnesium alumina spinel and/or Calcium aluminates, wherein the carrier has a pore volume 200-400 ml/kg and a BET surface area 2-50 m 2 /g,
modifying said carrier by a first impregnation with at least one alkaline earth metal in a first metal precursor solution,
decomposing the first metal precursor at a temperature of from 300-700° C. to form an alkaline earth metal oxide or alkaline earth metal hydroxide layer on the carrier, thereby obtaining a modified carrier,
carrying out a second impregnation by a second precursor solution comprising at least one metal Me in a second solution, the metal Me comprising a catalytic metal, wherein the second precursor solution is Me-nitrate, Me-citrate, Me-Ethylenediaminetetraacetic acid EDTA), or Me-Ethylenediamine (EDA), and
decomposing the second precursor to metal oxide, thereby obtaining a catalyst body having an enrichment of the at least one catalytic metal Me in an outer shell of the catalyst body, said at least one catalytic metal Me being present in a concentration having either an egg-shell profile and/or a hammock profile.
15. A process according to claim 14 , wherein the alkaline earth metal is selected from the group consisting of Mg, Ca and Ba.
16. A process according to claim 14 , wherein the catalytic metal Me is Ni, Ru and/or Rh.
17. A process according to claim 14 , wherein the second decomposition is carried out at 350-600° C.
18. A process according to claim 14 , wherein 90% of the catalytic metal Me present within an outer later having a thickness of up to 500 μm.
19. A process according to claim 14 , wherein the second impregnation is carried out by incipient wetness.
20. A process according to claim 14 , wherein the obtained catalyst body comprises a core section and the outer shell, wherein the core comprises carrier material impregnated with the alkali earth metal oxide or alkali earth metal hydroxide, wherein the outer shell comprises the carrier material impregnated with the alkali earth metal oxide or alkali earth metal hydroxide and the catalytic metal Me.
21. A process according to claim 14 , wherein the catalytic metal Me is Ni.