Integrated methods for chemical synthesis
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embodiment 1
2. The method of embodiment 1, wherein the syngas stream has a molar hydrogen to CO ratio between 0.5:1 and 1.2:1 and the upgraded gas stream has a hydrogen to CO ratio of at least 1.9:1.
3. The method of embodiment 1, wherein the second chemical process comprises Fischer Tropsch synthesis.
4. The method of embodiment 1, wherein the second chemical process comprises reaction on a fuel cell.
5. The method of embodiment 1, wherein the second chemical process comprises hydrogenation.
6. The method of embodiment 1, wherein the epoxide carbonylation product is selected from the group consisting of: optionally substituted beta lactone, optionally substituted succinic anhydride, and a polyester resulting from alternating polymerization of CO and the epoxide.
7. The method of embodiment 1, wherein the epoxide is ethylene oxide.
embodiment 7
8. The method of embodiment 7, wherein the carbonylation product is beta propiolactone.
9. The method of embodiment 7, wherein the epoxide carbonylation product is succinic anhydride and the upgraded gas stream has a molar hydrogen to CO ratio greater than 5:1.
embodiment 9
10. The method of embodiment 9, wherein and the upgraded gas stream has a hydrogen to CO ratio greater than 10:1, greater than 20:1, greater than 50:1, greater than 100:1, or greater than 1,000:1.
11. The method of embodiment 9, wherein the upgraded gas stream is substantially free of carbon monoxide.
12. Beta-propiolactone produced by carbonylation of ethylene oxide having a pMC of zero, as defined by ASTM D6866, using carbon monoxide having a pMC greater than zero, as defined by ASTM D6866.
13. Beta-propiolactone produced by carbonylation of ethylene oxide having a pMC greater than zero, as defined by ASTM D6866, using carbon monoxide having a pMC of zero, as defined by ASTM D6866.
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