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介绍了前处理-水解-生物接触氧化工艺处理染料废水的工程实例.当进水COD≤8000 mg/L时,出水可达到国家〈污水综合排放标准〉(GB8978-1996)二级标准. 相似文献
84.
Feiler U Ahlf W Hoess S Hollert H Neumann-Hensel H Meller M Weber J Heininger P 《Environmental science and pollution research international》2005,12(5):257-258
- In current biotest approaches, intact organisms or in vitro systems are exposed to sediments using different exposure scenarios.
The most important issue in sediment toxicity testing protocols is the question which test phase (solid or liquid) should
be used. Whole-sediment exposure protocols represent the most realistic scenario to simulate in situ exposure conditions in
the laboratory. However, until now there is no agreement in how to acquire and to evaluate the data of the various available
sediment contact assays. The SeKT joint research project was initiated with the aim to compare recently developed sediment
contact assays by addressing reference conditions, control sediments and toxicity thresholds for limnic sediment contact tests. 相似文献
85.
In this study,direct contact membrane distillation(DCMD)was used for treating fermentation wastewater with high organic concentrations.DCMD performance characteristics including permeate flux,permeate water quality as well as membrane fouling were investigated systematically.Experimental results showed that,after 12 hr DCMD,the feed wastewater was concentrated by about a factor of 3.7 on a volumetric basis,with the permeate flux decreasing from the initial 8.7 L/m~2/hr to the final 4.3 L/m~2/hr due to membrane fouling;the protein concentration in the feed wastewater was increased by about 3.5 times and achieved a value of 6178 mg/L,which is suitable for reutilization.Although COD and TOC in permeate water increased continuously due to the transfer of volatile components from wastewater,organic rejection of over 95%was achieved in wastewater.GC–MS results suggested that the fermentation wastewater contained 128kinds of organics,in which 14 organics dominated.After 12 hr DCMD,not only volatile organics including trimethyl pyrazine,2-acetyl pyrrole,phenethyl alcohol and phenylacetic acid,but also non-volatile dibutyl phthalate was detected in permeate water due to membrane wetting.FT-IR and SEM–EDS results indicated that the deposits formed on the membrane inner surface mainly consisted of Ca,Mg,and amine,carboxylic acid and aromatic groups.The fouled membrane could be recovered,as most of the deposits could be removed using a HCl/Na OH chemical cleaning method. 相似文献
86.
乌东矿急倾斜特厚煤层水平分段综放开采顶板破断特征研究 总被引:1,自引:0,他引:1
为研究急倾斜特厚煤层水平分段综放开采顶板破断特征,基于急倾斜特厚煤层工作面顶板赋存条件并结合弹性力学,建立了急倾斜特厚煤层水平分段开采顶板力学模型。通过力学模型分析,推导出急倾斜特厚煤层水平分段开采后顶板沿工作面倾向方向的岩板破断判据及挠度公式,应用三角级数方法对挠度公式进行求解,确定了顶板沿倾向方向上最大挠度发生的位置关系式。理论研究成果在乌东矿南采区B1+2急倾斜特厚煤层水平分段综放开采中的工程应用表明,工作面沿倾向方向上推进到385 m时顶板发生破断,倾向方向顶板最大挠度坐标位置为y=325.78 m,顶板沿工作面倾向方向的最大挠度位于采空区中部偏下位置。表现为急倾斜特厚煤层顶板在工作面上方的非对称性破断;相似材料试验进一步验证了顶板挠度公式的合理性。 相似文献
87.
分段进水生物接触氧化工艺处理河道污水的试验研究 总被引:6,自引:1,他引:5
选择滇池入湖污染负荷最高的大清河为对象,以分段进水生物接触氧化(SFBC)工艺对河道污水开展了分流处理的试验研究,已完成冬季枯水期、春季枯水期及夏季丰水期3个时期的研究.结果表明.SFBC工艺对水质变化具有很好的适应性,调整各时期的运行参数,可以使COD及TP的去除率分别稳定在50%和40%左右,但TN的去除受水温及溶解氧等的影响很大,在逐渐稳定后去除率可达到20%左右.接种活性污泥可以加快装置的启动.但总体去除效果不及来水自然驯化的污泥.随着运行时间延长以及来水带入河道底泥的影响.有无接种污泥在处理效率上的差别逐渐消失. 相似文献
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89.
采用机械破碎方式灭活活性污泥中高等微生物,并通过测定破碎前后泥样耗氧速率(OUR)之差别间接计算高等微生物的活性作用.实验结果表明,以分散机破碎活性污泥,高等微生物均可被有效地破碎灭活,且再培养138h后不再恢复.与此同时,对酵母菌破碎实验显示,机械破碎并未对其数量、形态以及活性产生太大影响,这表明机械破碎亦不会对个体尺寸比酵母菌更小的细菌构成任何影响.为使破碎前后活性污泥絮凝体形态基本一致,将破碎后的泥样经离心处理,以尽可能使絮凝体恢复如初(以SVI衡量).通过比较破碎前后泥样的OUR并计算可知,高等微生物活性相对于活性污泥总活性约占12%~14%. 相似文献
90.
Liquid water management is still a critical issue in the improvement of proton exchange membrane fuel cell (PEMFC) performance. In this work, for the first time, the liquid water behavior and transport inside the cathode of a PEMFC with a stirred tank reactor (STR) design, rather than the conventional PEMFC flow channel design, are numerically studied. The dynamic contact angle (DCA) is applied to multiple wall boundaries in the numerical model through a user-defined-function (UDF) code, i.e., STR-DCA model. Another numerical model with the static contact angle (SCA) and same operating conditions, i.e., STR-SCA model, is also developed for comparison. The volume of fluid (VOF) method is employed in the simulation to track the gas-liquid interface. The results show that the liquid water distribution and transport are significantly different between these two models, indicating the remarkable effects of DCA on the simulation results. It is also verified the capability of STR-PEMFC to reduce the liquid water flooding, showing the potential of this channel-less type fuel cell in the further development. 相似文献