Energy efficient synthesis of aliphatic aldehydes from alkenes and carbon dioxide
Provided is a process for producing an aldehyde from an alkylene. The process includes (a) photocatalytically dehydrogenating at least one alkane to obtain a mixture comprising at least one olefin and hydrogen, (b) adding carbon dioxide and hydrogen to the mixture, and (c) hydroformylating the olefin to at least one aldehyde. The process also includes converting carbon dioxide and hydrogen into water and carbon monoxide prior to the hydroformylating. In addition, the conversion of carbon dioxide and hydrogen into water and carbon monoxide is performed by a reverse water gas shift reaction.
1. A process for producing an aldehyde from an alkylene, the process comprising:
a) photocatalytically dehydrogenating at least one alkane to obtain a mixture comprising at least one olefin and hydrogen;
b) adding carbon dioxide and hydrogen to the mixture; and
c) hydroformylating the olefin to at least one aldehyde, and
further comprising converting carbon dioxide and hydrogen into water and carbon monoxide prior to the hydroformylating,
wherein the conversion of carbon dioxide and hydrogen into water and carbon monoxide is performed by a reverse water gas shift reaction.
2. The process of claim 1 , wherein
the alkane is n-butane,
the olefin is 1-butene, and
the aldehyde is valeraldehyde.
3. The process of claim 1 , wherein the conversion of carbon dioxide and hydrogen into water and carbon monoxide and the hydroformylating are performed in a conjoint reactor, over a conjoint catalyst, or both in a conjoint reactor and over a conjoint catalyst.
4. The process of claim 1 , wherein the photocatalytic dehydrogenating, the hydroformylating, or both, are performed by contacting a reactant with an immobilized catalyst.
5. The process of claim 4 , wherein the catalyst is immobilized using an ionic liquid.
6. The process of claim 5 , wherein the catalyst used for the photocatalytically dehydrogenating is supported by a porous glass.
7. The process of claim 4 , wherein the catalyst for the hydroformylating is a multinuclear ruthenium complex.
8. The of claim 1 , further comprising adding at least one salt during the hydroformylating.
9. The process of claim 1 , wherein the photocatalytic dehydrogenating is performed by contacting a reactant with an immobilized catalyst.
10. The process of claim 1 , wherein the hydroformylating is performed by contacting a reactant with an immobilized catalyst.
11. The process of claim 1 , wherein both the photocatalytic dehydrogenating and the hydroformylating are performed by contacting a reactant with an immobilized catalyst.
12. The process of claim 1 , wherein the conversion of carbon dioxide and hydrogen into water and carbon monoxide is performed by contacting the carbon dioxide and the hydrogen with an immobilized catalyst.
13. The process of claim 1 , wherein the photocatalytic dehydrogenating, the hydroformylating, and the conversion of carbon dioxide and hydrogen into water and carbon monoxide are each performed by contacting a reactant with an immobilized catalyst.
14. The process of claim 4 , wherein the conversion of carbon dioxide and hydrogen into water and carbon monoxide and the hydroformylating are performed in a conjoint reactor, over a conjoint catalyst, or both in a conjoint reactor and over a conjoint catalyst.
15. The process of claim 7 , wherein the multinuclear ruthenium complex is Ru 3 (CO) 12 .
16. The process of claim 8 , wherein the salt is selected from the group consisting of LiCl, LiBr, LiI, NaCl, and KCl.
17. The process of claim 1 , further comprising converting the carbon dioxide and hydrogen into water and carbon monoxide, wherein the converting and the hydroformylating are performed in a single reactor.
18. The process of claim 17 , wherein the converting and the hydroformylating are performed over a single catalyst.