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Valorization of calcium carbonate-based solid wastes for the treatment of hydrogen sulfide in a semi-continuous reactor: Part II - Slurry bubble column pilot

机译:基于碳酸钙的固体废物的储存用于半连续反应器中硫化氢的固体废物:第二部分 - 浆料泡沫柱飞行员

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摘要

This work is devoted to the removal of H2S from the gas phase using a suspension of calcium carbonate-based residues, recovered from the production of sodium bicarbonate. A 145 L (1.6 m height and 0.34 m internal diameter) slurry bubble column (SBC) reactor was used. The gaseous effluent was bed from the bottom and get out from the top of the column. The suspension (2-20 wt%) was recirculated from the bottom to the top by a pump. This created a counter-current regime between the gas phase (from the bottom to the top) and the liquid phase (from the top to the bottom) which favor the gas/liquid exchange inside the reactor. The influence of different parameters including solid concentration in the suspension (w(s)), recirculating rate of the suspension (Q(R)), inlet gas flow rate (Q(G)), and volume of the suspension, was investigated. The results obtained with this confirmed those at the lab scale, for both synthetic gaseous effluent (H2S diluted in compressed air) and real gaseous effluent emitted by the buffer tank of a wastewater treatment plant. This allows validating the technology before its deployment at the large industrial scale for H2S removal from the gas phase.
机译:使用碳酸钙基残留物的悬浮液从碳酸氢钠的碳酸氢钠中回收,该作品致力于从气相中除去H 2 S.使用145L(1.6米高和0.34米内径)浆料泡柱(SBC)反应器。气态流出物从底部均为床,从柱的顶部出来。悬浮液(2-20wt%)通过泵从底部到顶部再循环。这在气相(从底部到顶部)和液相(从顶部到底部的顶部)产生的逆流调节,这有利于反应器内的气体/液体交换。研究了不同参数在悬浮液中固体浓度的影响(W(s)),悬浮液的再循环率(Q(r)),入口气体流速(q(g))和悬浮液的体积。用这证实了实验室规模的结果,对于合成的气态流出物(在压缩空气中稀释的H 2 S稀释)和由废水处理厂的缓冲罐发射的真正的气态流出物。这允许在其在大型工业规模的部署之前验证该技术,以便从气相中移除H2S。

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