水解酸化-二级SBR-气浮工艺处理酱油废水研究

依托酱油废水实际处理工程 ,考察各处理单元中污泥驯化条件及CODCr、色度等的降解规律 ,重点研究SBR单元中pH、SVI、生物相等变化与出水水质的关系 ,探讨SBR污泥膨胀的原因及有效的控制手段。研究表明 ,进水CODCr为 30 0 0mg L、色度 5 0 0倍的酱油废水经“水解 二级SBR 气浮”工艺处理后 ,出水CODCr为 5 0mg L、色度 <5 0倍 ,达到国家一级排放标准     

SBR法处理工艺分类与应用

在归纳SBR法处理工艺分类的基础上，介绍各种SBR工艺处理难降解有机物的应用现状。     

SBR法在扬州啤酒厂废水处理中的应用

本文介绍用间歇式活性污泥(SBR)法处理啤酒生产废水。当废水COD_(cr)值在800～2000mg/L时,经SBR一级生化处理后的出水可达到国家规定的排放标准(GB8978-88)。将SBR工艺与可编程延时自动控制系统相结合,可简化操作。     

Process evaluation of an alternating aerobic-anoxic process applied in a sequencing batch reactor for nitrogen removal

In order to improve the nitrogen removal efficiency and save operational cost, the feasibility of the alternating aerobic-anoxic process (AAA process) applied in a sequencing batch reactor (SBR) system for nitrogen removal was investigated. Under sufficient influent alkalinity, the AAA process did not have an advantage over one aerobicanoxic (OAA) cycle on treatment efficiency because microorganisms had an adaptive stage at the alternating aerobic-anoxic transition, which would prolong the total cycling time. On the contrary, the AAA process made the system control more complicated. Under deficient influent alkalinity, when compared to OAA, the AAA process improved treatment efficiency and effluent quality with NH₄ ⁺-N in the effluent below the detection limit. In the nitrification, the average stoichiometric ratio between alkalinity consumption and ammonia oxidation is calculated to be 7.07 mg CaCO₃/mg NH₄ ⁺-N. In the denitrification, the average stoichiometric ratio between alkalinity production and NO₃ ⁻-N reduction is about 3.57 mg CaCO₃/mg NO₃ ⁻-N. As a result, half of the alkalinity previously consumed during the aerobic nitrification was recovered during the subsequent anoxic denitrification period. That was why the higher treatment efficiency in the AAA process was achieved without the supplement of bicarbonate alkalinity. If the lack of alkalinity in the influent was less than 1/3 of that needed, there is no need for external alkalinity addition and treatment efficiency was the same as that under sufficient influent alkalinity. Even if the lack of alkalinity in the influent was more than 1/3 of that needed, the AAA process was an optimal strategy because it reduced the external alkalinity addition and saved on operational cost. Translated from Acta Scientiae Circumstantiae, 2004, 24(4): 576–580 [译自: 环境科学学报]     

SBR法设计与运行控制模型的探讨

在综合分析了序批式活性污泥现行设计方法的基础上，根据生化反应动力学原理推导出ＳＢＲ系统设计的基本关系式，并用试验进行验证。据此总结出ＳＢＲ的优选设计方法，并进行评价和讨论。该设计方法引入了“进水期污泥负荷”和“反应期污泥负荷”两个概念。     

SBR工艺在脂肪酸废水处理工程中的应用

应用以生化处理为主体的工艺：厌氧-SBR法处理脂肪酸废水，通过治理工程实例运行，结果表明：工艺简单，占地面积小、基建投资少、运行费用低，处理后的出水水质稳定、处理效率高。     

混凝—SBR法处理城市垃圾填埋场渗滤液方法的研究

针对城市生活垃圾填埋场渗滤液的特点 ,提出了混凝—SBR法处理工艺。试验结果表明 ,经该工艺处理的垃圾渗滤液各项指标可达国家规定的排放标准     

高含硫味精废水处理的研究

采用吹脱－混凝－厌氧消化－两段ＳＢＲ－絮凝沉淀工艺处理味精废水，试验结果表明，当进水ＣＯＤ为２２３５１ｍｇ／Ｌ，ＳＯ＾２－４５１００００ｍｇ／Ｌ，ＮＨ３－Ｎ７５７１ｍｇ／Ｌ、色度（倍）３９０６和ＰＨ１．３时，出水ＣＯＤ９９ｍｇ／Ｌ、ＳＯ＾２－４９５ｍｇ／Ｌ、ＮＨ３－Ｎｌｍｇ／Ｌ色度１６和ＰＨ６．５，其水质均达到ＧＢ８９７８－１９９６规定的一级排放标准。     

SBR的反硝化吸磷脱氮现象研究

通过改变生物除磷脱氮工艺SBR(A／O／A／O)的运行参数，对其缺氧段进行研究，发现：进入缺氧段的聚磷菌体内的PHB是否充足，是缺氧吸磷现象是否明显的关键。在SBR的缺氧段也存在反硝化吸磷现象，此反应装置的活性污泥中含有大量的可利用NO3^-作为电子受体，进行缺氧反硝化吸磷的反硝化聚磷菌(DPB)。     

套筒式SBR滗水器的设计与运行

文章重点介绍套筒式滗水器的设计及应用.套筒式滗水器由撇水堰槽、下降套筒管、水平管、传动装置等部分组成,通过下降管中内外套筒上下伸缩,撇水堰槽上下移动,将表层澄清水撇入滗水器,再经下降管汇入水平管,最后从出水管排出.此种滗水器具有运行稳定、控制简单、不漏水、水流运动平稳、不扰动污泥层等特点.