Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Carbon Dioxide | HCID 280 | — |
| Reactant | Methane | HCID 297 | — |
| Reactant | Ethane | HCID 6324 | — |
| Reactant | Ethylene | HCID 6325 | — |
| Reactant | 2,6-Diethylaniline | HCID 11369 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Reactant | HCID 178418416 | HCID 178418416 | — |
| Solvent | Water | HCID 962 | — |
| Product | 7-Ethylindole | HCID 2724711 | — |
Reaction Steps
The reactor for the dehydrocyclization contained 0.5 liter of Cu-chromite/BaO catalyst in table form (4×4 mm). The reactor was heated to 660° C. and was fed 68 g of 2,6-diethylaniline and 81 g of water per hour. After cooling, a mixture of a heavily organic phase and of a lighter water phase, as well as a waste (discharge) gas, was obtained in the recipient vessel. The waste gas had the following typical composition (vol. percent): 80.0 percent of hydrogen; 2.9 percent of methane; 2.0 percent of ethane; 0.4 percent of ethylene; 2.0 percent of carbon monoxide; and 10.7 percent of carbon dioxide. Obtained per hour were 38 l of waste gas, 59 g of organic raw product and 76 g of water which can be used again. The organic raw product had the following composition:
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04703126 |
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| Source dataset | uspto-grants-1987_10 |
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| ORD ID | ord-6c4411e1892b4f8188cd1ada033a70ad |
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| Source note | uspto-grants-1987_10 |
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