Systems and methods for on-site liquid alcohol production from carbon dioxide
Methods for producing alcohols by deriving carbon dioxide from air or another dilute source, and supplying water, which is converted to hydrogen and oxygen, with subsequent conversion of the carbon dioxide and hydrogen into alcohols is disclosed. The method includes, but is not limited to including, a direct air capture system carbon dioxide, a water electrolysis unit powered by electricity, a hydrogenation reactor to convert carbon dioxide and hydrogen gases into alcohols, and a distillation system to separate alcohols or a single constituent alcohol from other hydrogenation products. Optionally, these methods may include systems capture water from air, if water or hydrogen is not available on-site, and the distillation system may use propylene glycol as an extraction solvent. This process can be used for on-site production of feedstock alcohols such as ethanol at high purity, and many other applications.
1. A system for production of alcohols, comprising:
an electrolyzer configured to convert water to hydrogen and oxygen;
a hydrogenation reactor comprising a first catalyst configured to convert carbon dioxide to a mixture of alcohols, wherein the mixture of alcohols comprises ethanol; and
wherein the first catalyst comprises nanoparticles comprising copper and zinc.
2. The system of claim 1 , wherein the hydrogenation reactor operates with selectivity for the ethanol among liquid products of greater than 10% by volume.
3. The system of claim 1 , wherein the hydrogenation reactor operates with selectivity for the ethanol among liquid products of greater than 30% by volume.
4. The system of claim 1 , wherein the first catalyst comprises CuZn, CuZnFeK, CuZnFeKC, CuZnFeAlK, CuZnFeNa, CuZnFeCoK, CuZnFeCoNaK, or CuZnK, optionally on an alumina support.
5. The system of claim 1 , wherein the first catalyst further comprises sodium.
6. The system of claim 1 , further comprising an apparatus for capturing carbon dioxide from an input stream.
7. The system of claim 6 , wherein the input stream is air.
8. The system of claim 1 , wherein the first catalyst further comprises cobalt, selenium, sodium, potassium, iron, molybdenum, sulfur, oxygen, or alloys or chemical compounds thereof.
9. The system of claim 8 , wherein the first catalyst comprises CuZnFeK, CuZnFeKC, CuZnFeAlK, CuZnFeNa, CuZnFeCoK, CuZnFeCoNaK, or CuZnK, optionally on an alumina support.
10. The system of claim 1 , wherein the first catalyst comprises CuZn, optionally on an alumina support.
11. The system of claim 1 , wherein the first catalyst comprises CuZnFeK, optionally on an alumina support.
12. The system of claim 1 , wherein the first catalyst comprises CuZnFeKC, optionally on an alumina support.
13. The system of claim 1 , wherein the first catalyst comprises CuZnFeAlK, optionally on an alumina support.
14. The system of claim 1 , wherein the first catalyst comprises CuZnFeNa, optionally on an alumina support.
15. The system of claim 1 , wherein the first catalyst comprises CuZnFeCoK, optionally on an alumina support.
16. The system of claim 1 , wherein the first catalyst comprises CuZnFeCoNaK, optionally on an alumina support.
17. The system of claim 1 , wherein the first catalyst comprises CuZnK, optionally on an alumina support.
18. The system of claim 1 , further comprising a distillation system.