Mechanisms of granular activated carbon anaerobic fluidized-bed process for treating phenols wastewater

ＩｎｔｒｏｄｕｃｔｉｏｎＢｅｆｏｒｅｔｈｅ 1 980ｓｃｏｎｖｅｎｔｉｏｎａｌｔｒｅａｔｍｅｎｔｐｒｏｃｅｓｓｅｓｏｆｐｈｅｎｏｌｓｗａｓｔｅｗａｔｅｒａｒｅｓｏｌｖｅｎｔｅｘｔｒａｃｔｉｏｎ ,ｐｈｙｓｉｃａｌａｄｓｏｒｐｔｉｏｎ ,ｃｈｅｍｉｃａｌｏｘｉｄａｔｉｏｎａｎｄａｅｒｏｂｉｃｂｉｏｌｏｇｉｃａｌｐｒｏｃｅｓｓ.Ａｍｏｎｇｔｈｅｂｉｏｌｏｇｉｃａｌｕｎｉｔｐｒｏｃｅｓｓｅｓａｃｔｉｖａｔｅｄｓｌｕｄｇｅｐｒｏｃｅｓｓｉｓｍａｉｎｏｎｅ.Ａｆｔｅｒｔｈｅ 1 980ｓａｎａｅｒｏｂｉｃｂｉｏｌｏｇｉｃ…     

厌氧—好氧—生物炭系统处理印染废水实例

阐述了采用厌氧水解－好氧生物接触－生物炭吸附氧化工艺处理印染废水的工艺流程、原理、工艺参数及特点。该系统对印染废水ＣＯＤｃｒ及色度的处理取得良好效果，且污泥量少，节省了污泥处理费用。     

氧化塘离散数的研究

对模型氧化塘离散数d进行了相似分析,结果表明,模型塘的离散数d可以推广到原型中去.在试验资料基础上,提出了计算氧化塘离散数d值的经验公式,该公式反映了氧化塘内的极慢流动特征.应用该公式预测了有横向导流墙时氧化塘内的离散数,与试验结果符合较好.     

三唑磷农药废水厌氧处理可行性研究

采用厌氧流化率工艺处理在唑磷农药废水，必须降低原水中ＮＨ３－Ｎ含量，调整营养比例，当ＣＯＤ：Ｎ：Ｐ＝（１８０～２００）：５：１时，在中温厌氧消化条件下，ＣＯＤ含量可从４１７０ｍｇ／ｌ，去除率约５０％，沼气产率达到０．２５６ｍ＾３／ｍ＾３．ｄ。因此，把厌氧处理作为好氧处理的预处理单元，能确保整个处理系统出水达标。     

微量营养物质对有机废水厌氧消化过程的调控作用

通过向处理酸性葡萄酒蒸馏废水的厌氧移动床生物膜反应器中投加微量营养物质的试验,得出利用微量营养物质调控厌氧消化过程在技术上是可行的。Fe、Ni、Co组合不仅能加快挥发性有机酸(VFA),特别是丙酸的降解速率,进而提高厌氧反应器的溶解COD去除率,同时,还有利于厌氧反应器有机负荷的快速提升和较强pH缓冲能力的形成。B族维生素对厌氧移动床生物膜反应器运行效果影响不大。Fe对厌氧移动床生物膜反应器运行有一定影响,但效果也不十分明显。     

镧、铈对厌氧颗粒污泥产甲烷的Hormesis效应及其动力学研究

间歇培养条件下研究了单一稀土元素镧(La3 )和铈(Ce3 )在不同浓度水平下对厌氧颗粒污泥活性及其动力学行为的影响.结果表明,La3 和Ce3 对厌氧颗粒污泥比产甲烷活性有促进作用的浓度范围均为0.01～0.1 mg·L-1,促进作用浓度峰值均为0.05mg·L-1,最大促进百分比分别为10.35%和20.79%;La3 和Ce3 对SMA(比甲烷活性)的半抑制浓度分别为5mg·L-1和1000mg·L-1,La3 较易对污泥产生抑制作用.米-门方程可以用来描述厌氧消化过程中甲烷发酵阶段的动力学行为,稀土元素La3 和Ce3 投加至反应系统后,提高了甲烷发酵过程的动力学常数Vmax和半饱和常数Ks.     

氧化塘处理高速公路服务区污水技术初探

提出并试验研究了氧化塘处理高速公路服务区污水的方法，所得结果可用于高等级公路服务区及管理区污水处理。     

长炼第二污水处理场氧化沟工艺运行小结

臭伯尔氧化沟池容大，停留时间长，运行稳定，对氧化沟污泥培养及开工运行进行了小结，并结合运行过程中的几个问题进行了分析和探讨。     

气浮--厌氧--生物接触氧化工艺处理屠宰废水

介绍了采用气浮-厌氧-生物接触氧化工艺处理屠宰废水的工程实例。当进水CODcr≤4500mg／L时，出水可达到国家《肉类加工工业污染物排放标准》(GB13457—1992)一级标准。     

Effect of Cross-Linking Waste Protein with Dialdehydes on Its Biodegradation Under Anaerobic Conditions

Most native polymers used in processing and application technologies are admittedly disposable from the environment in a biologic manner, but products possess low mechanical strength. One of the paths to increasing this attribute (if feasible) is their cross-linking, which may, however, affect their readiness to biodegradation. In the presented work this condition was observed on the example of waste protein (Hykol B) cross-linking by means of glutardialdehyde and glyoxal. Degree and course of cross-linking were determined through impedance spectroscopy. The objective of this work also was to obtain data for constructing a sensor capable of following the cross-linking course in real time, for potential industrial application of Hykol in continuous production. Impedance spectroscopy proved to be applicable even to this kind of material marked by considerable water content and exhibiting relatively high electric conductivity; so far it had been used only for materials of low conductivity. An aqueous environment inoculated with digested anaerobic sludge from a municipal wastewater treatment plant was selected for modeling anaerobic conditions. The relation was studied between cross-linking degree given by content of cross-linking agent (determined by impedance spectroscopy) and biodegradation degree under anaerobic conditions. It was confirmed that network density as given by quantity of added agent not only reduced breakdown degree but also slowed the course of the process. This fact is particularly obvious with cross-linking by means of glyoxal; network density is thus dependent on type of employed substance, which affect type and structure of created network. That not merely forms an obstacle during polymer swelling and dissolution but also prevents access of bacteria to source of metabolized organic carbon.