Abietanes and methods of making and using the same
US-2025154106-A1 · May 15, 2025 · US
US11724971B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11724971-B2 |
| Application number | US-202017634879-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 12, 2020 |
| Priority date | Aug 14, 2019 |
| Publication date | Aug 15, 2023 |
| Grant date | Aug 15, 2023 |
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Processes of making [1.1.1]propellane utilize reaction conditions that include reacting 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane with an effective amount of solid magnesium.
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What is claimed is: 1. A process of making [1.1.1]propellane, comprising reacting 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane with an effective amount of solid magnesium under substantially anhydrous reaction conditions that are selected to produce [1.1.1]propellane. 2. The process of claim 1 , wherein the substantially anhydrous reaction conditions comprise reacting 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane with the solid magnesium in the presence of an aprotic ether solvent that comprises tetrahydrofuran. 3. The process of claim 2 , wherein the aprotic ether solvent further comprises an ether selected from diethylether, diethoxymethane, dibutylether, methyl tert-butyl ether, dioxane, 2-methyltetrahydrofuran, cyclopentyl methyl ether, and mixtures thereof. 4. The process of claim 2 , wherein the aprotic ether solvent further comprises a hydrocarbon solvent for the 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane and the [1.1.1]propellane. 5. The process of claim 4 , wherein the hydrocarbon solvent is selected from toluene and heptane. 6. The process of claim 4 , further comprising filtering a reaction mixture resulting from the reacting to thereby at least partially remove at least one insoluble salt. 7. The process of claim 1 , wherein the effective amount of the solid magnesium is a molar excess that is at least 2×with respect to 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane. 8. The process of claim 1 , wherein the substantially anhydrous reaction conditions are further selected to produce a yield of the produced [1.1.1]propellane that is about 10% or higher. 9. The process of claim 8 , wherein the yield is about 20% or higher. 10. The process of claim 8 , wherein the yield is about 30% or higher. 11. The process of claim 8 , wherein the yield is about 40% or higher. 12. The process of claim 8 , wherein the yield is about 50% or higher. 13. The process of claim 1 , wherein the substantially anhydrous reaction conditions comprise a reaction temperature in the range of about 0° C. to about 85° C. 14. The process of claim 1 , wherein the substantially anhydrous reaction conditions comprise a reaction time in the range of about 30 minutes to about 10 hours. 15. The process of claim 1 , further comprising separating at least a portion of the produced [1.1.1]propellane from a reaction mixture containing the 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane and the solid magnesium. 16. The process of claim 1 , comprising contacting at least about one kilogram of 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane with the effective amount of solid magnesium. 17. The process of claim 1 , further comprising purifying the produced [1.1.1]propellane to provide a purified [1.1.1]propellane that has a purity of about 90% or higher. 18. The process of claim 17 , wherein the purity is about 95% or higher. 19. The process of claim 18 , wherein the purity is about 99% or higher. 20. The process of claim 1 , wherein the substantially anhydrous reaction conditions comprise a batch condition. 21. The process of claim 1 , wherein the substantially anhydrous reaction conditions comprise a continuous flow reaction condition conducted in a continuous flow reactor.
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