稠油污水的有机组成及可生化性研究

采用物化-厌氧-好氧法处理稠油污水,对物化生化处理各阶段出水的有机组分进行定性分析,并对稠油污水的可生化性进行了进一步研究。研究结果表明:不同处理工序出水的有机成分差异较大,经过气浮、厌氧处理后,稠油污水可生化性逐步提高,有利后续好氧生物处理。     

利用A/O技术处理己内酰胺生产废水的研究

探讨采用先进的A/O(厌氧菌 /好氧菌 )生物脱氮技术对己内酰胺生产废水进行处理的工作机理和工艺设计方法 ,分析了温度、溶解氧、pH值、进水碳氮比等参数对生物脱氮工艺过程的影响 ,并对其关键技术进行了研究     

有机垃圾厌氧发酵产氢技术研究进展

利用有机垃圾产氢的研究逐渐兴起,人们利用有机垃圾产氢既可以最大程度地使有机垃圾资源化,减少环境的污染,又可以通过无污染氢气的获得改善能源市场,缓解能源的压力。分析了国内外厌氧发酵产氢的技术现状;以厌氧发酵产氢的原理和机理入手,讨论微生物、发酵过程、过程参数等对产氢效率和速率的影响;最后还对厌氧发酵产氢的可行性进行研究。     

作物秸秆能源转化技术研究进展

利用作物秸秆生产可再生能源是解决秸秆环境污染和开辟新的能量资源的重要途径之一。作物秸秆能源转化技术主要有热解气化、厌氧消化、液化、乙醇化、直接燃烧和固化等。简要介绍了我国作物秸秆的资源量及利用现状,着重对国内外作物秸秆能源转化技术的发展、研究现状及工业化应用情况进行了详细介绍。通过对各技术特点和存在问题的分析,探讨了未来发展趋势。建议加强作物秸秆液化与乙醇化技术的系统性研究以及工艺过程的开发。     

UASB-接触氧化处理高浓度有机废水试验研究

本文主要通过UASB 接触氧化生化处理模型对某化工厂废水的试验研究，探索运用UASB法处理高浓度有机废水的可行性。同时还探讨了废水的CODcr及含盐量对UASB处理效率的影响，以及关键参数的选用。     

Denitrifying phosphorous removal in anaerobic/anoxic SBR system with different startup operation mode

To achieve stable and efficient nitrogen and phosphorus removal and to investigate the characteristics of the A/A SBR enriched with denitrifying phosphorus removal bacteria(DPB),the whole course of startup was studied with two reactors operated in different mode.The reactor I was operated under anaerobic/settling/anoxic/settling mode,and the reactor II was operated under anaerobic/anoxic/settling mode.Differences between the two reactors in removal efficiency of COD,nitrogen and phosphorus were examined.The results indicated that efficient performance could be achieved in both reactors with different startup operation mode,while the phosphorus removal efficiency was improved sooner in reactor I than in reactor II,which suggested that reactor I would supply a more favorable condition for DPB proliferation.Meanwhile,it was observed that the amount of organic substrates consumption had a linear correlation to that of phosphorus release in anaerobic phase when DPB was accumulated in the A/A SBR denitrifying phosphorus removal system.     

Treatment of methanol wastewater with two-stage and two-phase anaerobic process

The two-stage and two-phase anaerobic process (TSTP) composed of hydrolytic acidification reactor,first-order and second-order external circulation anaerobic reactors (EC) was taken to treat methanol wastewater. Test results show that TSTP process is quick start-up in 51 d, and the maximum VFA of hydrolytic acidification reactor effluent reaches 876 mg/L. Under the condition of volume loading of 6.56 kgCOD/m3·d, COD removal rate of the first-order EC reactor is about 85%, and under the condition of volume loading of 1.02 kgCOD/m3·d, COD removal rate of the second-order EC reactor is about 50%. When the inflow COD of TSTP process is between 7000-11000 mg/L, its effluent COD is lower than 600 mg/L. In the biological conversion process of methanol into methane,the production of acetic acids as an intermediate product can be ignored and the direct production of methane from methanol is predominant.     

Development of a novel modified EGSB reactor for municipal sewage treatment at ambient temperatures

A novel modified expanded granular sludge bed(EGSBm) reactor was developed for anaerobic treatment of municipal sewage with mixed liquid recirculation instead of effluent recirculation commonly adopted by a conventional EGSB(EGSBc) reactor.Performances of these two reactors were compared in treating municipal sewage at ambient temperatures ranging from 8 to 26 ℃.At an upflow liquid velocity(Vup) of 10.3 m/h,the mean concentrations of filtrated COD(CODfilt) and COD of the EGSBm effluent were determined to be 59.4 and 95.9 mg/L,respectively,which were significantly lower than those of the EGSBc effluent operated under identical experimental conditions.When the organic loading rate was suddenly increased from 1.2 to 7.2 kg COD/(m3·d),the EGSBm regained the removal efficiency of previous operation phase in 10 d.Hydrodynamic characteristics of the reactors were compared using the residence time distribution(RTD) model.It was found that the treatment efficiency of EGSBm kept increasing as the Vup increased.The polymerase Chain Reaction-Denaturing Gradient Gel Electrophoresis(PCR-DGGE) technique was used to analyze the microbial diversity in EGSBm.Fingerprinting pattern indicated that some species in the inoculating sludge were still reserved in the granular sludge of EGSBm,moreover,several new species occurred.     

污泥吸附动力学与平衡模型的实验研究

采用好氧和厌氧污泥进行污泥的生物吸附实验,研究好氧与厌氧污泥吸附动力学和吸附平衡模型。研究表明:好氧和厌氧污泥的吸附过程中,颗粒内扩散是污泥吸附的主要限速阶段,但它不是唯一的限速因素。好氧和厌氧污泥的假二级反应模型比一级、二级反应模型更能描述污泥的吸附过程。Langmuir和Freundlich的吸附平衡方程都适合描述厌氧和好氧污泥的吸附平衡过程。     

厌氧附着膜膨胀床处理生活废水的研究

文章利用厌氧附着膜膨胀床（AAFEB）反应器处理生活废水。选择合适的活性污泥和活性炭载体,在60d内反应器启动挂膜完成。实验表明,此反应器能够有效的去除生活废水中的有机物,出水水质良好,反应器运行稳定。通过稳定床层膨胀率在10％-20％,研究水力停留时间（HRT）和温度对CODCr去除率的影响,得到该反应器的最佳工艺条件为,HRT8h,温度控制在28℃,在此工艺条件下,CODCr的去除率在85％以上,BOD5的去除率在73％以上,且SS的去除率在75％以上。