Low temperature sulfur tolerant tar and sulfur removal with concomitant synthesis gas conditioning
View Patent ↗A catalyst comprising of NiO; Al 2 O 3 ; and ZnO. The catalyst is capable of greater than 5% sulfur removal from a synthesis gas at a temperature range from 300° C. to 600° C.
1. A process of removing tar compounds from synthesis gas, the process comprising:
producing a tar-containing synthesis gas;
producing a treated synthesis gas by contacting the tar-containing synthesis gas with a first catalyst comprising:
(a) NiO;
(b) Al 2 O 3 ; and
(c) ZnO,
introducing the treated synthesis gas to a further catalytic chemical reaction;
wherein the synthesis gas is not heated prior to contact with the first catalyst and the treated synthesis gas is not cooled prior to undergoing the further catalytic chemical reaction.
2. The process of claim 1 , wherein the temperature range in which the synthesis gas is contacted with the catalyst is from 350° C. to 550° C.
3. The process of claim 1 , wherein the NiO is present from 1 to 10 wt %.
4. The process of claim 1 , wherein the catalyst is capable of greater than 5% sulfur removal from a synthesis gas at a temperature range from 300° C. to 600° C.
5. The process of claim 1 , wherein the catalyst is capable of removing tar from the synthesis gas at quantities greater than 55% conversion at 350° C.
6. The process of claim 4 , wherein the contacting is at a pressure in the range from 14.7 to 1,200 psig.
7. The process of claim 4 , wherein the contacting is at a pressure in the range from 250 to 1,000 psig.
8. The process of claim 4 , wherein the catalyst simultaneously removes the tar from the tar-containing synthesis gas during the contacting.
9. The process of claim 1 , wherein the first catalyst comprises 0.5 to 15 wt % ZnO.
10. A process of:
producing a raw synthesis gas containing tar compounds and sulfur containing compounds by gasification;
producing a treated synthesis gas by contacting the raw synthesis gas with a first catalyst comprising:
(a) NiO present from 1 to 10 wt %;
(b) Al 2 O 3 ; and
(c) ZnO,
wherein the catalyst is capable of greater than 20% sulfur removal from a synthesis gas while simultaneously removing 20% to 60% of the tar from the raw synthesis gas at a temperature range from 350° C. to 550° C. and a pressure range from 14.7 to 1,200 psig; and
introducing the treated synthesis gas to a subsequent catalytic chemical reaction;
wherein the synthesis gas is not heated prior to contact with the first catalyst and the treated synthesis gas is not cooled prior to undergoing the subsequent catalytic chemical reaction.
11. The process of claim 10 , wherein the first catalyst comprises 0.5 to 15 wt % ZnO.