Removing ammonia from skim by air stripping with rotating packed bed

Based on the effects of skim components on ammonium removal as well as the current processing technology, a new process-intensified technology of removing ammonia from skim by air stripping on rotating packed bed was proposed. The experiments were conducted on a wave-thread packed Rotating Packed Be...

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Veröffentlicht in:Chinese journal of chemical engineering 2019-03, Vol.27 (3), p.528-533
Hauptverfasser: Gui, Hongxing, Li, Xiuping
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container_title Chinese journal of chemical engineering
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creator Gui, Hongxing
Li, Xiuping
description Based on the effects of skim components on ammonium removal as well as the current processing technology, a new process-intensified technology of removing ammonia from skim by air stripping on rotating packed bed was proposed. The experiments were conducted on a wave-thread packed Rotating Packed Bed (RPB) under atmospheric pressure, suggesting that, in terms of order of importance, the ammonium concentration of feed-stock (xw), the average ultra-gravity factor (β), feed-stock flux (L), and gas flux (G) had significant impact on ammonium removal rate (η) and the ammonium concentration of products (xD). In the experiment, mass-transfer coefficient in gas phase (kyae) increases with the increase of β, G/L, and L. The ammonium concentration of products decreases with the increase of β, G/L and the increase of L. The ammonium concentration of products would be as low as 0.10% and the ammonia removal rate would be 63.21% when skim temperature was 25 °C, xw 0.28%, β 133.2, and G/L 15.0 m3·L−1. Experiment results indicated that the proposed technology for removing ammonium from skim on a rotating packed bed would be a new process-intensified technique compared with traditional aeration process and centrifugal atomization method.
doi_str_mv 10.1016/j.cjche.2018.06.027
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The experiments were conducted on a wave-thread packed Rotating Packed Bed (RPB) under atmospheric pressure, suggesting that, in terms of order of importance, the ammonium concentration of feed-stock (xw), the average ultra-gravity factor (β), feed-stock flux (L), and gas flux (G) had significant impact on ammonium removal rate (η) and the ammonium concentration of products (xD). In the experiment, mass-transfer coefficient in gas phase (kyae) increases with the increase of β, G/L, and L. The ammonium concentration of products decreases with the increase of β, G/L and the increase of L. The ammonium concentration of products would be as low as 0.10% and the ammonia removal rate would be 63.21% when skim temperature was 25 °C, xw 0.28%, β 133.2, and G/L 15.0 m3·L−1. 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subjects Air stripping
Ammonia removal
Skim
Ultra-gravity technology
title Removing ammonia from skim by air stripping with rotating packed bed
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