Compounds having two or more exovinylene cyclocarbonate units
US-10604500-B2 · Mar 31, 2020 · US
US11292780B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11292780-B2 |
| Application number | US-201816634255-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 14, 2018 |
| Priority date | Aug 14, 2017 |
| Publication date | Apr 5, 2022 |
| Grant date | Apr 5, 2022 |
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The present invention relates to a process for preparing cyclic carbonates of formula Ia or Ib or mixtures thereof (Ia) (Ib) comprising the process step: a) reacting a propargylic alcohol of formula II (II) with carbon dioxide in the presence of at least one transition metal catalyst TMC1, which comprises a transition metal selected from metals of groups 10, 11 and 12 of the periodic table of the elements according to IUPAC and at least one bulky ligand.
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The invention claimed is: 1. A process for preparing a cyclic carbonate of formula Ia or Ib or a mixture thereof wherein R 1 is hydrogen or an organic radical having from 1 to 40 carbon atoms, the process comprising: a) reacting a propargylic alcohol of formula II wherein R 1 is defined as in formula Ia or Ib, with carbon dioxide in the presence of at least one transition metal catalyst TMC1, which comprises: a transition metal selected from metals of groups 10, 11 and 12 of the periodic table of the elements; and at least one bulky ligand selected from the group of ligands consisting of a compound of formula III and a compound of formula IV wherein D is P, As or Sb, R 2 , R 3 , R 4 and R 5 are each independently an organic radical having from 1 to 40 carbon atoms, and Z is a divalent bridging group selected from —CR 7 ═CR 8 —, —CR 7 ═N—, —CR 7 R 9 — CR 8 R 10 — and —CR 7 R 9 —CR 8 R 10 —CR 11 R 12 —, wherein R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are each independently hydrogen or an organic radical having from 1 to 40 carbon atoms or two adjacent radicals R 7 and R 8 and/or R 10 and R 11 together with the atoms connecting them form a monocyclic or polycyclic, substituted or un-substituted, aliphatic or aromatic ring system which has from 4 to 40 carbon atoms and optionally comprises at least one heteroatom selected from the group of elements consisting of Si, Ge, N, P, O and S thereby obtaining the cyclic carbonate of formula Ia or Ib or the mixture thereof in a yield of from 2% to 99%. 2. The process of claim 1 , wherein R 1 is hydrogen, hydroxymethyl (—CH 2 OH), acetoxy-methylene (—CH 2 OC(O)CH 3 ), formyloxy-methylene (—CH 2 OC(O)H) or —CH 2 OC(O)OCH 3 . 3. The process of claim 1 , wherein the transition metal of the at least one transition metal catalyst TMC1 is Ag. 4. The process of claim 1 , wherein the at least one transition metal catalyst TMC1 is prepared in situ by using a transition metal compound, which does not comprise any bulky ligand, and the compound of formula III or the compound of formula IV as a bulky ligand or a protonated form of the compound of formula IV represented by formula V, wherein R 2 , R 5 and Z are defined as in formulae III or IV and X − is an anion equivalent, together with a base. 5. The process of claim 4 , wherein the transition metal compound is selected from AgOAc, AgF, Ag 2 O and Ag 2 CO 3 . 6. The process of claim 1 , wherein the at least one bulky ligand is a compound of formula III. 7. The process of claim 1 , wherein the at least one bulky ligand is selected from a compound of the following formulae A to P and mixtures thereof 8. The process of claim 1 , wherein a molar ratio of the at least one bulky ligand to the transition metal of the at least one transition metal catalyst TMC1 is in a range of from 0.4 to 1.2. 9. The process of claim 1 , wherein an amount of the at least one transition metal catalyst TMC1 used in a) is in a range of from 0.005 to 5 mol %, based on an amount of the propargylic alcohol of formula II. 10. The process of claim 1 , wherein a) is performed at a pressure in a range of from 1 to 50 bar. 11. The process of claim 1 , wherein a) is performed at a temperature in a range of from 0° C. to 1° *C. 12. The process of claim 1 , wherein a) is carried out in the presence of a solvent selected from the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, halogenated hydrocarbons, amides, ureas, nitriles, sulfoxides, sulfones, esters, carbonates, ethers, alcohols and mixtures thereof. 13. The process of claim 1 , wherein the cyclic carbonate of formula Ia or Ib or the mixture thereof is separated from the at least one transition metal catalyst TMC1 after a) via distillation. 14. The process of claim 1 , wherein the the at least one transition metal catalyst TMC1 is recycled to the reacting of a) after the cyclic carbonate of formula Ia or Ib or the mixture thereof is removed via distillation. 15. A process for preparing a cyclic carbonate of formula Ia or Ib or a mixture thereof wherein R 1 is hydrogen or an organic radical having from 1 to 40 carbon atoms, the process comprising: a) reacting a propargylic alcohol of formula II wherein R 1 is defined as in formula Ia or Ib, with carbon dioxide in the presence of at least one transition metal catalyst TMC1, which comprises: a transition metal selected from metals of groups 10, 11 and 12 of the periodic table of the elements; and at least one bulky ligand selected from the group of ligands consisting of a compound of formula III and a compound of formula IV wherein D is P, As or Sb, R 2 , R 3 , R 4 and R 5 are each independently an organic radical having from 1 to 40 carbon atoms, and Z is a divalent bridging group selected from —CR 7 ═CR 8 —, —CR 7 ═N—, —CR 7 R 9 — CR 8 R 10 — and —CR 7 R 9 —CR 8 R 10 —CR 11 R 12 —, wherein R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are each independently hydrogen or an organic radical having from 1 to 40 carbon atoms or two adjacent radicals R 7 and R 8 and/or R 10 and R 11 together with the atoms connecting them form a monocyclic or polycyclic, substituted or un-substituted, aliphatic or aromatic ring system which has from 4 to 40 carbon atoms and optionally comprises at least one heteroatom selected from the group of elements consisting of Si, Ge, N, P, O and S, wherein the at least one transition metal catalyst TMC1 is prepared in situ by using a transition metal compound, which does not comprise any bulky ligand, and the compound of formula III or the compound of formula IV as a bulky ligand or a protonated form of the compound of formula IV represented by formula V, wherein R 2 , R 5 and Z are defined as in formulae III or IV and X − is an anion equivalent, together with a base. 16. A process for preparing a cyclic carbonate of formula Ia or Ib or a mixture thereof wherein R 1 is hydrogen or an organic radical having from 1 to 40 carbon atoms, the process comprising: a) reacting a propargylic alcohol of formula II wherein R 1 is defined as in formula Ia or Ib, with carbon dioxide in the presence of at least one transi
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Organic electrolyte · CPC title
Unsaturated compounds used as ligands · CPC title
Vinylene carbonate; Substituted vinylene carbonates · CPC title
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