首页> 外文会议>Biennial conference of the International Association on Water Quality >SPECIFIC OXYGEN UPTAKE, NITRIFICATION AND DENITRIFICATION RATES OF A ZINC-ADDED ANOXIC/OXIC ACTIVATED SLUDGE PROCESS
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SPECIFIC OXYGEN UPTAKE, NITRIFICATION AND DENITRIFICATION RATES OF A ZINC-ADDED ANOXIC/OXIC ACTIVATED SLUDGE PROCESS

机译:锌添加的缺氧/氧化活性污泥法的特定氧吸收,硝化和反硝化速率

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The specific oxygen uptake rate (SOUR), specific nitrification rate (SNR) and specific denitrification rate (SDNR) of an anoxic-oxic activated sludge process fed with zinc-added synthetic wastewaters were investigated. Two different characteristics of synthetic wastewaters were used, i.e., 500 mg/l COD, 40 mg/l TKN and 10 mg/l P (representing normal COD load) for Model A while 3500 mg/l COD, 175 mg/l TKN and 25 mg/l P (representing high COD load) for Model B. The zinc doses varied from 0 (control) to 10, 25, 35 and 50 mg/l. When the two systems reached steady states, they were further shocked with 300 mg/l zinc for 4 consecutive days before returning to their initial conditions. The SRT and F/M ratio of both models were 10 days and 0.26-0.47 day~(-1), respectively. The endogenous SOURs of both models were not much affected by the increase of zinc concentration. They were about 7.5 to 10 and 9.4 to 11.5 mg O_2/g MLSS-hr, for Models A and B, respectively. In Model A, as the zinc increased from 0 to 50 mg/l, the SNRs dropped from 4.0 to 1.4 mg NH_4~+-N /g MLSS-hr whereas the initial SDNRs fell from 19.6 to 5.3 mg NO_3~- /g MLSS-hr. Meanwhile, the SNRs of Model B were relatively constant (1.5-1.8 mg NH_4~+-N /g MLSS-hr) while the initial SDNRs dropped from 16.2 to 8.3 mg NO_3~- /g MLSS-hr. That is, under high COD load conditions, the zinc dose applied here did not significantly affect the carbon removing heterotrophs and nitrifiers while a slight effect was seen on the denitrifiers and significant retardation was observed for both nitrifiers and denitrifiers in case of normal COD load. During the shock period, the SNRs of Model A dropped to 0.67 to 1.26 mg NH_4~+-N /g MLSS-hr whereas the initial SDNRs decreased drastically to 1.5 to 3.0 mg NO_3~- /g MLSS-hr. The impact from the zinc shock in such circumstances was obviously higher on the denitrifiers than on the nitrifiers. In Model B, the SNRs were 0.77 to 1.5 mg NH_4~+-N /g MLSS-hr and the initial SDNRs were 2.9 to 6.18 mg NO_3~- /g MLSS-hr. Not much effect on nitrifiers was evident in this case. For Model A, the recoverability of the heterotrophs and the nitrifiers was not so good, while that of the denitrifiers was quite satisfactory. However for Model B, those recuperation abilities were comparable for all three organisms. The data therefore suggested that there may be some differences in the species domain between the carbon removing microorganisms and the denitrfiers, however, further investigations for confirmation are required.
机译:研究了添加锌的合成废水处理的缺氧-含氧活性污泥工艺的比耗氧率(SOUR),比硝化率(SNR)和比反硝化率(SDNR)。对于模型A,使用了两种不同的合成废水特性,即500 mg / l COD,40 mg / l TKN和10 mg / l P(代表正常COD负荷),而3500 mg / l COD,175 mg / l TKN和模型B为25 mg / l P(代表高COD负荷)。锌剂量从0(对照)到10、25、35和50 mg / l不等。当两个系统达到稳定状态时,连续4天用300 mg / l的锌进一步震惊,然后恢复到初始状态。两种模型的SRT和F / M比分别为10天和0.26-0.47天〜(-1)。两种模型的内源性SOUR并不受锌浓度增加的太大影响。对于模型A和模型B,它们分别约为7.5至10和9.4至11.5 mg O_2 / g MLSS-hr。在模型A中,随着锌从0增加到50 mg / l,SNR从4.0降至1.4 mg NH_4〜+ -N / g MLSS-hr,而初始SDNRs从19.6降至5.3 mg NO_3〜-/ g MLSS -hr。同时,模型B的SNR相对恒定(1.5-1.8 mg NH_4〜+ -N / g MLSS-hr),而初始SDNRs从16.2降至8.3 mg NO_3〜-/ g MLSS-hr。也就是说,在高COD负载条件下,此处施用的锌剂量不会显着影响除碳异养菌和硝化器,而对反硝化器影响很小,并且在正常COD负载情况下,对于硝化器和反硝化器均观察到明显的阻滞作用。在冲击期间,模型A的SNR下降至0.67至1.26 mg NH_4〜+ -N / g MLSS-hr,而初始SDNRs急剧下降至1.5至3.0 mg NO_3〜-/ g MLSS-hr。在这种情况下,锌冲击对反硝化器的影响明显大于对硝化器的影响。在模型B中,SNR为0.77至1.5 mg NH_4〜+ -N / g MLSS-hr,初始SDNR为2.9至6.18 mg NO_3〜-/ g MLSS-hr。在这种情况下,对硝化器的影响不明显。对于模型A,异养菌和硝化器的可回收性不是很好,而反硝化器的可回收性却很令人满意。但是对于模型B,所有三种生物的恢复能力均相当。因此,数据表明除碳微生物和反硝化剂之间在物种域上可能存在一些差异,但是,需要进行进一步的研究以确认。

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