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Pretreatment of anaerobic digestion effluent with ammonia stripping and biogas purification

机译:氨汽提和沼气净化对厌氧消化废水的预处理

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In this study, ammonia stripping was optimized for pretreating anaerobic digestion effluent from an anaerobic digestion plant, and the possibility of using CO_2 stripping and biogas injection for adjusting the pH of the effluent before and after the ammonia stripping process was also investigated. For ammonia stripping, the results showed that an overdose of calcium hydroxide, i.e., 27.5 g/L wastewater, achieved higher ammonia, phosphorus, chemical oxygen demand, suspended solids, and turbidity removal efficiency. An air flow rate of 5 L/min for 1L of wastewater was thought as suitable for engineering application. The pH of the anaerobic digestion effluent can be increased from about 7 to about 9 by CO_2 stripping, however which is insufficient for ammonia stripping. For 1L of wastewater treated after ammonia stripping, the pH can be neutralized to about 7 from greater than 11 through biogas injection at 1 L/min for less than 30 min, and continuous injection does not decrease the pH. It was roughly estimated that 43 m~3 of biogas (CH_4:CO_2≈ 60%:40%) produced daily could be purified to CH_4:CO_2 ≈ 74%:26% by neutralizing the pH of the 5 m~3 anaerobic digestion effluent pretreated by ammonia stripping.
机译:在这项研究中,优化了氨汽提工艺以预处理厌氧消化厂的厌氧消化液,并研究了在氨汽提工艺之前和之后使用CO_2汽提和沼气注入来调节废水pH值的可能性。对于氨汽提,结果表明过量的氢氧化钙,即27.5 g / L废水,获得了更高的氨,磷,化学需氧量,悬浮固体和浊度去除效率。 1L废水的空气流速为5 L / min被认为适合工程应用。可以通过CO_2汽提将厌氧消化废水的pH从约7增加到约9,但这不足以进行氨汽提。对于在氨气汽提后处理的1L废水,可通过以1 L / min的速度注入沼气少于30分钟将pH从大于11的pH中和至大约7。粗略估计,通过中和5 m〜3厌氧消化液的pH值,可以将每日产生的43 m〜3沼气(CH_4:CO_2≈60%:40%)纯化为CH_4:CO_2≈74%:26%。通过氨汽提预处理。

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