May I ask how the flow rates in various pipelines are controlled during hydrogen peroxide production? Thank you.
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How can control be implemented to maintain stable liquid levels in various locations? For example, when using a hydrogenated clay bed, what level should the working fluid be at in order not to affect the entire system? Thank you.
Based on your total volume, generally about 10% of the hydrogenated liquid coming out of the liquid-liquid separator goes into the clay bed
Oh, thank you. I’m feeling very dizzy today. By the afternoon at work, the effluent separator contained a lot of water; the boundary between the working fluid and water wasn’t clear, with plenty of working fluid dispersed in the water. What could be causing this? Today, it seemed to me that the flow rate from the phosphoric acid metering tank was almost half faster than usual – could that be the reason? Also, the alkali tower had too much alkali, and it couldn’t be completely drained. The specific gravity of the alkali was 1.284 after using freshly distilled alkali. We drained that alkali into the working fluid storage tank and then pumped it directly into the working fluid reservoir, but the liquid level in the alkali tower didn’t rise. Is this approach appropriate? What factors are responsible for the working fluid carrying away the alkali from the alkali tower? Thank you.