Abstract
1. Experiments on the conversion of natural gas on a pilot plant which reproduces the process completely have shown that a high conversion level is possible. The residual methane content is 0.4–0.8% vol. for a specific crude supply rate of 3000–5000 cm3/g · h. 2. It has been shown that a highly efficient separation of the catalyst from the heat transfer agent is possible under actual operating conditions.
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