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Solutions to a combined problem of excessive hydrogen sulfide in biogas and struvite scaling

机译:沼气中过量硫化氢和斯特鲁维缩放的硫化氢结合问题的解决方案

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摘要

The Woodman Point Wastewater Treatment Plant (WWTP) in Western Australia has experienced two seperate problems causing avoidable maintenance costs: the build-up of massive struvite (MgNH4PO4′ 6H2O) scaling downstream of the anaerobic digester and the formation of hydrogen sulfide (H2S) levels in the digester gas to levels that compromised gas engine operation and caused high operating costs on the gas scrubber. As both problems hang together with a chemical imbalance in the anaerobic digester, we decided to investigate whether both problems could be (feasibly and economically) addressed by a common solution (such as dosing of iron solutions to precipitate both sulfide and phosphate), or by using separate approaches. Laboratory results showed that, the hydrogen sulfide emission in digesters could be effectively and economically controlled by the addition of iron dosing. Slightly higher than the theoretical value of 1.5 mol of FeCl3 was required to precipitate 1 mol of dissolved sulfide inside the digester. Due to the high concentration of PO43- in the digested sludge liquor, significantly higher iron is required for struvite precipitation. Iron dosing did not appear an economic solution for struvite control via iron phosphate formation. By taking advantage of the natural tendency of struvite formation in the digester liquid, it is possible to reduce the risk of struvite precipitation in and around the sludge-dewatering centrifuge by increasing the pH to precipitate struvite out before passing through the centrifuge. However, as the Mg2+/PO43- molar ratio in digested sludge was low, by increasing the pH alone (using NAOH) the precipitation of PO43- was limited by the amount of cations (Ca2+ and Mg2+) available in the sludge. Although this would reduce struvite precipitation in the centrifuge, it could not significantly reduced PO43- recycling back to the plant. For long-term operation, maximum PO43- reduction should be the ultimate aim to minimise PO43- accumulation in the plant. Magnesium hydroxide liquid (MHL) was found to be the most cost-effective chemical to achieve this goal. It enhanced struvite precipitation from both, digested sludge and centrate to the point where more than 95% PO43- reduction in the digested sludge was achieved.
机译:西澳大利亚州的伍德曼角废水处理厂(WWTP)经历了两个单独的问题,导致可避免的维护成本:厌氧消化池下游结垢的大型鸟粪石(MgNH4PO4'6H2O)堆积和硫化氢(H2S)水平的形成沼气池中的汽油会降低到损害燃气发动机运行并导致煤气洗涤塔运行成本高的水平。由于这两个问题都与厌氧消化池中的化学物质不平衡有关,我们决定研究是否可以通过一种通用的解决方案(例如定量注入铁溶液以沉淀硫化物和磷酸盐的方法)来解决(可行且经济)这两个问题。使用不同的方法。实验室结果表明,添加铁计量可以有效,经济地控制消化池中的硫化氢排放。为了在蒸煮器内沉淀出1摩尔溶解的硫化物,需要略高于1.5摩尔的FeCl3的理论值。由于消化的污泥液中PO43-的浓度很高,鸟粪石沉淀所需的铁明显更高。通过磷酸铁的形成来控制鸟粪石的投加铁似乎不是经济的解决方案。通过利用消化池液体中鸟粪石形成的自然趋势,可以通过增加pH值使鸟粪石在通过离心机之前沉淀出来,从而降低污泥脱水离心机内部及其周围鸟粪石沉淀的风险。但是,由于消化污泥中Mg2 + / PO43-的摩尔比很低,仅通过增加pH值(使用NAOH),PO43-的沉淀就受到污泥中阳离子(Ca2 +和Mg2 +)含量的限制。尽管这会减少鸟粪石在离心机中的沉淀,但不能显着减少PO43的循环再造。对于长期运行,最大程度地减少PO43-应该是减少工厂中PO43-积累的最终目标。氢氧化镁液体(MHL)被发现是实现这一目标的最具成本效益的化学物质。它增强了消化污泥和浓缩物中鸟粪石的沉淀,使消化污泥中的PO43减少了95%以上。

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