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Ammonia and pH Inhibition in Anaerobic Treatment of Wastewaters, Part I: Experimental

机译:厌氧处理废水中的氨和pH抑制,第一部分:实验

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The influences of pH and ammonia on methane production in the anaerobic treatment of an acetic-propionic-butyric acid mixture in batch reactors operated at 37℃ were investigated. Two independent sets of experiments were carried out using seeds from two different full-scale industrial anaerobic treatment reactors. One of the seeds ("Sludge A") was obtained from an upflow anaerobic sludge-blanket (UASB) reactor treating the waste from a potato chips production plant. The second sludge seed ("Sludge B") was from an expanded granular sludge-blanket (EGSB) reactor treating a corn processing waste. Experiments were carried out at four different pH values (6.8, 7.4, 7.8, 8.4) and with six different TAN (Total Ammonia Nitrogen) values (262 mg/L (control), 1000, 1500, 2000, 2500, 3000). Three vials (triple runs) were used for each pH and TAN value. The sludge seeds used in the inhibition tests were not exposed to high levels of ammonia at any stage before the tests. For each vial, cumulative methane production was monitored for a period long enough for the termination of biogas production. Although neither sludge was acclimated to ammonia, the lag-phase times were less than 2 days for Sludge A and essentially zero for Sludge B for all TAN and pH values. At certain high pH and high TAN values, however, methanogenic activity ceased within about 1–3 months; and then activity restarted and methane formation rate reached its maximum values after this period. If the experiments had not been continued following this period, this reactivation phenomenon would not have been detected.
机译:研究了37℃间歇反应器中乙酸-丙酸-丁酸混合物厌氧处理过程中pH和氨水对甲烷生成的影响。使用来自两个不同的大型工业厌氧处理反应器的种子进行了两组独立的实验。一种种子(“污泥A”)是从上流厌氧污泥毯(UASB)反应器中获得的,该反应器处理了薯片生产厂的废物。第二种污泥种子(“污泥B”)来自处理玉米加工废料的膨化颗粒污泥毯(EGSB)反应器。在四个不同的pH值(6.8、7.4、7.8、8.4)和六个不同的TAN(总氨氮)值(262 mg / L(对照),1000、1500、2000、2500、3000)下进行实验。每个pH和TAN值使用三个小瓶(三次运行)。抑制试验中使用的污泥种子在试验前的任何阶段均未暴露于高水平的氨中。对于每个小瓶,监测甲烷的累积生产时间足够长,以终止沼气生产。尽管两种污泥都无法适应氨,但是对于所有TAN和pH值,污泥A的滞后时间均少于2天,而污泥B的滞后时间基本上为零。但是,在一定的高pH和高TAN值下,产甲烷活性在大约1-3个月内就停止了。在此期间之后,活动重新开始,甲烷形成速率达到最大值。如果在此期间未继续进行实验,则不会检测到这种重新激活现象。

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