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Simultaneous Sludge Disintegration and Carbon Source Generation for Enhanced Biological Phosphorous Removal Using Ozonation

机译:同时进行污泥分解和碳源生成,以利用臭氧增强生物除磷

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One of the major drawbacks of wastewater treatment is the amount of excess sludge produced,which depends on the type of process applied. Since the quantities of sludge produced in a typicalactivated sludge process are considerable, it has a strong impact on the cost of sludge treatmentand final disposal. The sludge treatment and disposal from an activated sludge process can makeup to 60% of the total wastewater treatment operational cost (Inchauste-Daza et al., 2011). Theozonation of the excess sludge is considered to be one of the extensively studied and successfullyapplied methods for sludge reduction (Chu et al., 2009; Inchauste-Daza et al., 2011). Whensludge is ozonated, a new carbon source is formed and it has been reasoned that due to its newcharacteristics of biodegradability it may be consumed by the microorganisms such as by PAOs(bio-P organisms) in enhanced biological phosphorous removal (EBPR). However, theinvestigation of the use of ozonated sludge as substrate in nutrient removal is limited. Two typesof experiments have been carried out- ozonation tests of activated sludge, and biological activitytests for enhanced biological phosphorous removal. The ozonation of sludge resulted in thereduction of both MLSS and MLVSS; and it is evident from the trend that the volatile fraction isdisintegrated and becomes soluble making the trend of both close to parallel. It has been observedthat while the amount of residual biosolids drops with ozone dose increase, the soluble fractionrises; and the mineralized fraction becomes more significant.The results with acetate (HAc) as carbon source show that during the anaerobic phase all thesubstrate was consumed and stored by PAOs in the first 20 minutes; the poly-P internally storedwas effectively used as energy, releasing up to 3.30 mg PO_4-P/g VSS at the end of the anaerobicphase. In the following stage, PAOs did not uptake all the phosphorus, and thus the specific Puptake was found to be 3.19 mg PO_4-P/g VSS at the end of the tests. The results fromdisintegrated sludge use indicate that the ozonated sludge at various ozone doses were certainlyused by PAOs during the anaerobic phase. However, not all substrates were identically used. Thehighest specific P-release was found to be 2.78 mg PO_4-P/g VSS, with a rate of 5.52 mg PO_4-P/gVSS·h, when using ozonated sludge at higher dose of 0.13 g O_3/g MLSS as substrate. The resultsindicate that the properties of the carbon source present in the ozonated sludge are promising; thewastewater treatment plants can be integrated with sludge ozonation to significantly reduce theamount of sludge generation and external chemical (carbon source) requirement.
机译:废水处理的主要缺点之一是产生的过量污泥量大, 这取决于所应用的过程类型。由于典型情况下产生的污泥量 活性污泥工艺相当多,对污泥处理成本有很大影响 和最终处置。活性污泥工艺产生的污泥处理和处置可以使 高达废水处理总运营成本的60%(Inchauste-Daza等人,2011年)。这 过量污泥的臭氧化被认为是广泛研究和成功的方法之一 减少污泥的实用方法(Chu等人,2009; Inchauste-Daza等人,2011)。什么时候 污泥被臭氧处理,形成了新的碳源,并且据推测,由于其新的 生物可降解性的特征,可能会被微生物(例如PAO)消耗 (bio-P生物)中增强的生物除磷(EBPR)。但是,那 使用臭氧化污泥作为基质去除营养的研究非常有限。两种类型 进行了许多实验,研究了活性污泥的臭氧化测试以及生物活性 增强生物除磷的测试。污泥的臭氧化导致了 减少了MLSS和MLVSS;从趋势可以明显看出,挥发分是 崩解并变得可溶,使两者的趋势接近平行。已经观察到 当残留生物固体的数量随着臭氧剂量的增加而下降时,可溶部分 上升矿化的部分变得更重要。 以醋酸盐(HAc)为碳源的结果表明,在厌氧阶段,所有 在最初的20分钟内,底物被PAO消耗并存储;内部存储的poly-P 被有效地用作能量,在厌氧结束时释放高达3.30 mg PO_4-P / g VSS 阶段。在接下来的阶段,PAOs不会吸收所有磷,因此特定的P 在测试结束时,摄取量为3.19 mg PO_4-P / g VSS。结果来自 分解污泥的使用表明,各种臭氧剂量下的臭氧化污泥肯定是 在厌氧阶段由PAO使用。但是,并非所有基材都被相同地使用。这 发现最高的P释放量为2.78 mg PO_4-P / g VSS,比率为5.52 mg PO_4-P / g VSS·h,当使用更高剂量的臭氧化污泥(0.13 g O_3 / g MLSS)作为底物时。结果 表明存在于臭氧污泥中的碳源的性质是有前途的;这 废水处理厂可与污泥臭氧化处理相结合,以显着减少废水的排放 污泥产生量和外部化学物质(碳源)需求。

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