硝酸盐电子受体反硝化同时除磷试验分析

经研究发现AAA SBR系统中的活性污泥可以利用硝酸盐作为电子受体进行缺氧吸磷并同时发生反硝化脱氮。试验利用“双泥”系统进一步探讨了污水生物反硝化同时除磷的可能性,结果表明 :“双泥”系统的“双重”吸磷以及内碳源反硝化除磷方式可以使生物处理出水磷酸盐浓度趋近于零,TP≤ 0 2 3mg L、NH3 N≤ 0 5mg L、TN≤ 8mg L、CODCr≤2 5mg L。     

生物除磷脱氮工艺技术研究

采用厌氧－缺氧－好氧工艺（简称Ａ２／Ｏ工艺）,研究除磷脱氮的主要影响因素及其规律。结果表明,ＣＯＤ／ＴＰ值增大,总磷去除率提高,但当ＣＯＤ／ＴＰ＞６０时,提高缓慢;硝酸盐的存在对除磷有抑制;ＣＯＤ／ＴＫＮ＜１０时,总氮去除率随碳氮比增大而增加,大于此值几乎无影响;混合液回流比小于３时,回流比的变化对总磷总氮的去除均有影响;温度对脱氮的影响比除磷显著,小于１５℃氮去除率明显下降,而８～１０℃时仍有较好的除磷效果。     

Biomass from phytopathogens and culture conditions improve Penicillium chrysogenum antimicrobial activity and antifungal compounds production

The present study evaluated the effect of culture conditions and phytopathogenic strain co-culture on the production of antimicrobial metabolites and antifungal activity of Penicillium chrysogenum R1, which PCR identified. Antimicrobial activity was determined using the Hunter-Hunter experimental design with three factors (pH, incubation temperature, and inoculum, at two levels each). The antifungal metabolites, β 1-3 glucanase and chitinase, produced in the presence of live and inactivated Fusarium oxysporum Fsox C11 biomass, were evaluated using HPLC-MS and GC-MS. Results showed that P. chrysogenum inhibited the growth of five phytopathogenic fungal strains, and the most significant inhibition was observed for F. oxysporum Fsox C11. The best conditions to achieve the highest antifungal activity of the cell-free extract were pH 7, 28°C, 1 × 10⁶ spores/mL, and 144 h of fermentation, observing 86% inhibition of F. oxysporum Fsox C11 growth. Production of antifungal metabolites such as 1,4-benzoquinone imine, viridicatic acid, phenol-5-methyl-2-(1-methyl ethyl), and hydrolytic enzymes β 1-3 glucanase and chitinase was detected. The results define the perspective in designing new processes and products for biocontrol phytopathogens.     

影响生物滤池氧传递速率的几个因素

充足的氧气是进行好氧处理的保证,在传统的生物滤池中,靠的是自然通风供氧,供氧的好坏直接影响到生物滤池处理的效率.探讨了影响氧传递速率的因素,以供环境工程设计者参考.     

燃煤电厂排放PAHs的气粒分配机制和排放通量

对循环流化床锅炉(CFB)布袋除尘器进口和出口的多环芳烃(PAHs)进行了分析,研究了PAHs在气相和颗粒相中的分配机理.结果表明,除尘过程气相和颗粒相PAHs对应的去除率分别为45.59％与70.67％～89.06％.气相中主要为低分子量PAHs,颗粒相中主要为高分子量PAHs.随着粒径的增加,低分子量PAHs比例呈...     

颗粒活性炭载体新型生物转盘去除生活污水中COD和NH3-N的研究

开发一种改进型生物转盘处理生活污水,将盘片改为转笼状,并向其中加入颗粒活性发作为载体,研究该系统对生活污水的处理效果。结果表明：在转盘转速为15rpm和HRT分别为10h、8h、6h、4．5h情况下,进水COD平均浓度约为223mg／L,出水COD平均浓度分别为15．6、17．9、23．4、28．2mg/L,平均去除率为93．0％、91．9％、89．5％、86．6％;进水NH3-N平均浓度约为22mg／L,出水NH3-N平均浓度分别为0．32、1．13、2．30、5．71mg／L,平均去除率为98．5％、94．8％、89．7％、74．6％。     

川西地区气田废水处理技术及应用

简要介绍了川西地区气田废水的水质特征,阐述了物理及化学处理、生物处理、气田废水回注在川西地区的应用,其中齐福废水处理站经过物理及化学处理之后、袁家废水处理站经过生物处理后,基本达到了《污水综合排放标准》(GB8978-1996),并对川西气田废水处理技术的发展做了展望。     

炼油污水深度处理回用的中试

采用两级曝气生物滤池和多介质滤池相串联的中试装置,连续处理某炼油厂污水车间二浮出水,主要考察了中试装置对污水中主要污染物的去除效果和规律,并确定了适宜的气水比。试验结果表明:采用该工艺时,除石油类外,其它各项指标都达到《循环冷却水用再生水水质标准》(HG/T3923-2007)要求的水质指标;两级曝气生物滤池的气水比分别选用5.6∶1和5∶1为宜;验证了BAF是通过生物氧化和过滤两种作用来去除COD,第一段BAF以去除污水中碳化有机物为主,第二段BAF主要以去除污水中的NH4+-N为主。     

钻井废液毒性检测与评价研究

以几种典型钻井液体系为研究对象,分别选用成熟可靠的检测方法对其生物毒性、化学毒性和重金属含量进行分析,结果表明:部分钻井废液具有一定生物和化学毒性,其中,磺化体系钻井液在生物毒性和化学毒性方面均超标,应重点加强管理;低密度无固相体系和磺化体系钻井液中Hg和Cr元素存在不同程度的超标。     

Biogas combustion in a chemical looping fluidized bed reactor

Chemical looping combustion (CLC) is a process in which oxygen required for combustion of a fuel is supplied by the metal oxide. Metal oxide plays the role of an oxygen carrier by providing oxygen for combustion when being reduced and is then re-oxidized by air in a separate reactor. Combustion is thus without any direct contact between air and fuel: as a consequence flue gas does not contain nitrogen of air which simplifies flue gas treatment prior to sequestration. In the present study, biogas combustion was analyzed in a chemical looping combustion fluidized bed reactor. NiAl_0.44O_1.67 and Cu_0.95Fe_1.05AlO₄ metal oxide particles were used as oxygen carriers. The experiments have shown the feasibility of biogas combustion in chemical looping combustion: CH₄ of the biogas was completely converted to CO₂ and H₂O with a small fraction of CO and H₂. The outlet flue gas distribution profile was not affected by ageing during the cycles of reduction and oxidation, indicating the chemical stability of the oxygen carriers. There was limited formation of carbon on the oxygen carriers during reduction.