Conversion of mixed methane/ethane streams
The invention relates to a process for conversion of a stream comprising methane and ethane, comprising converting ethane from a stream comprising methane and ethane, in which stream the volume ratio of methane to ethane is of from 0.005:1 to 100:1, to a product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere; separating the product having a vapor pressure at 0° C. lower than 1 atmosphere from the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane; and chemically converting methane from the stream comprising methane, or feeding methane from the stream comprising methane to a network that provides methane as energy source, or liquefying methane from the stream comprising methane.
1. A process for conversion of a stream comprising methane and ethane, comprising
converting ethane from a stream comprising methane and ethane, in which stream the volume ratio of methane to ethane is of from 0.005:1 to 100:1 to a product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere comprising ethylene oxide converted from ethylene produced as an intermediate product of the conversion step;
separating the product having a vapor pressure at 0° C. lower than 1 atmosphere from the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane; and
chemically converting methane from the stream comprising methane or feeding methane from the stream comprising methane to a network that provides methane as energy source, or liquefying methane from the stream comprising methane.
2. The process according to claim 1 , wherein when converting ethane to the product having a vapor pressure at 0° C. lower than 1 atmosphere, the conversion of ethane is higher than 30%.
3. The process according to claim 1 , wherein the volume ratio of any recycled portion of the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere to the non-recycled portion of said stream is of from 0:1 to 0.5:1.
4. The process according to claim 1 , comprising
subjecting a stream comprising methane and ethane, in which stream the volume ratio of methane to ethane is of from 0.005:1 to 100:1 to oxydehydrogenation conditions resulting in a stream comprising methane, ethylene and optionally acetic acid;
converting ethylene from the stream comprising methane, ethylene and optionally acetic acid to a product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere;
separating the product having a vapor pressure at 0° C. lower than 1 atmosphere from the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere, resulting in a stream comprising methane; and
chemically converting methane from the stream comprising methane or feeding methane from the stream comprising methane to a network that provides methane as energy source, or liquefying methane from the stream comprising methane.
5. The process according to claim 4 , wherein when subjecting the stream comprising methane and ethane to oxydehydrogenation conditions, the conversion of ethane is higher than 30%.
6. The process according to claim 4 , wherein the volume ratio of any recycled portion of the stream comprising methane, ethylene and optionally acetic acid resulting from the first conversion step to the non-recycled portion of said stream is of from 0:1 to 0.5:1.
7. The process according to claim 4 , wherein the stream comprising methane and ethane has a volume ratio of methane to ethane is from 0.2:1 to 100:1.
8. The process according to claim 4 , wherein the stream comprising methane and ethane has a volume ratio of methane to ethane from 0.5:1 to 100:1.
9. The process according to claim 4 , wherein the conversion of ethane is from 50 to 99.9%.
10. The process according to claim 4 , wherein the conversion of ethane is from 60 to 99.9%.
11. The process according to claim 4 , wherein the conversion of ethane is from 70 to 99.9%.
12. The process according to claim 4 , wherein the conversion of ethane is from 70 to 90%.
13. The process according to claim 4 , wherein the volume ratio of any recycled portion of the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere to the non-recycled portion of said stream is 0:1 to 0.2:1.
14. The process according to claim 4 , wherein the volume ratio of any recycled portion of the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere to the non-recycled portion of said stream is 0.1.
15. The process according to claim 1 , wherein the stream comprising methane resulting from separating the product having a vapor pressure at 0° C. lower than 1 atmosphere from the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere, additionally comprises unconverted ethylene and/or carbon oxides and is subjected to hydrogenation resulting in a stream comprising methane and optionally ethane.
16. The process according to claim 1 , wherein the volume ratio of methane to ethane is from 0.2:1 to 100:1.
17. The process according to claim 1 , wherein the volume ratio of methane to ethane is from 0.5:1 to 100:1.
18. The process according to claim 1 , wherein the conversion of ethane is from 50 to 99.9%.
19. The process according to claim 1 , wherein the conversion of ethane is from 60 to 99.9%.
20. The process according to claim 1 , wherein the conversion of ethane is from 70 to 99.9%.
21. The process according to claim 1 , wherein the conversion of ethane is from 70 to 90%.
22. The process according to claim 1 , wherein the volume ratio of any recycled portion of the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere to the non-recycled portion of said stream is 0:1 to 0.2:1.
23. The process according to claim 1 , wherein the volume ratio of any recycled portion of the stream comprising methane and the product having a vapor pressure at 0° C. lower than 1 atmosphere to the non-recycled portion of said stream is 0:1.