The issue of non-catalytic pure oxygen partial oxidation of coke oven gas
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I am working on a process plan for the utilization of coke oven gas, and I would like to ask fellow experts questions related to the non-catalytic partial oxidation process using pure oxygen for coke oven gas: 1. What is the appropriate conversion pressure? Is around 3 kilograms sufficient? 2. Is this technology mature? Could you provide suppliers for this process? 3. Can an output of 80,000 cubic meters per hour be handled by a single furnace? 4. Are there any requirements regarding the gas composition and impurities for this process? 5. Other relevant information. Thank you all for your help!
Follow-up question: Can the heavy components in coke oven gas, such as benzene, tar, and naphthalene, also be converted after the transformation?