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181.
采用连续流生物活性炭(BAC)工艺处理水中挥发性苯系物(BTEX,包括苯、甲苯、乙苯、二甲苯),评价进水负荷、活性炭炭型等因素对于BAC处理性能的影响.研究表明,在40d的处理时间内,除苯之外,其余BTEX的BAC出水中均未检出苯系物(进水为6mg/L).为了检验BAC在高BTEX负荷情况时的处理效果,将进水浓度设定为19~32mg/L左右,在EBCT为1.2min条件下同样只有苯的出水浓度上升至10mg/L(C/Cin为0.45),然后略有下降,最终保持在5~10mg/L(C/Cin为0.3以下),其余苯系物出水浓度均一直保持小于5mg/L.这表明BAC可以有效地处理高负荷BTEX(8.68~12.9kgTOC/(m3·d))的进水.生物活性炭对于活性炭吸附容量的恢复有比较明显的作用,煤质炭和椰壳炭的生物再生效率分别为53.6%和26.6%,煤质炭再生效率高的原因可能是其具备更多的大型中孔和大孔. 相似文献
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针对大蒜废水特点,采用了铁屑微电解-UASB-接触氧化工艺进行处理.运行结果表明:在设计进水水质、水量范围内,COD、BOD5、氨氮和ss去除率分别为98%、99%、70%和98%,出水各项指标均达到GB 8978--1996<污水综合排放标准>中的一级排放标准,系统运行费用为1.19元/m3. 相似文献
185.
印钞废水属高浓度难降解有机废水,对环境污染严重。鉴于现有处理工艺出水普遍不达标的情况,通过对比实验确定了改进方案:超滤浓缩液离心出水在进入接触氧化池前,增加新的处理单元(Fenton氧化-混凝)。Fenton氧化最佳条件:FeSO4.7H2O投加量14 g/L,H2O2的投加量34 mL/L,初始pH值6.0,氧化反应时间1.5h,温度18.8℃;混凝过程最佳条件:PAC投加量4 g/L,PAM(5‰)投加量10 mg/L,pH值7。新增单元对废水中COD去除率接近80%,可生化性提高1.6倍,色度降低36%。 相似文献
186.
Pretreatment of thickened waste activated sludge (TWAS) by combined microwave and alkaline pretreatment (MAP) was studied to
improve thermophilic anaerobic digestion efficiency. Uniform design was applied to determine the combination of target temperature
(110–210°C), microwave holding time (1–51 min), and NaOH dose (0–2.5 g NaOH/g suspended solids (SS)) in terms of their effect
on volatile suspended solids (VSS) solubilization. Maximum solubilization ratio (85.1%) of VSS was observed at 210°C with 0.2
g-NaOH/g-SS and 35 min holding time. The effects of 12 different pretreatment methods were investigated in 28 thermophilic batch
reactors by monitoring cumulative methane production (CMP). Improvements in methane production in the TWAS were directly related
to the microwave and alkaline pretreatment of the sludge. The highest CMP was a 27% improvement over the control. In spite of the
increase in soluble chemical oxygen demand concentration and the decrease in dewaterability of digested sludge, a semi-continuous
thermophilic reactor fed with pretreated TWAS without neutralization (at 170°C with 1 min holding time and 0.05 g NaOH/g SS)
was stable and functioned well, with volatile solid (VS) and total chemical oxygen demand (TCOD) reductions of 28% and 18%,
respectively, which were higher than those of the control system. Additionally, methane yields (L@STP/g-CODadded, at standard
temperature and pressure (STP) conditions of 0°C and 101.325 kPa) and (L@STP/g VSadded) increased by 17% and 13%, respectively,
compared to the control reactor. 相似文献
187.
Aged refuse from waste landfills closed for eight years was examined and found to contain rich methanotrophs capable of biooxidation
for methane. Specially, community structure and methane oxidation capability of methanotrophs in the aged refuse were
studied. The amount of methanotrophs ranged 61.97 103–632.91 103 cells/g (in dry basis) in aged refuse from Shanghai Laogang
Landfill. Type I and II methanotrophs were found in the aged refuse in the presence of sterilized sewage sludge and only Type I
methanotrophs were detected in the presence of nitrate minimal salt medium (NMS). The clone sequences of the pmoA gene obtained
from the aged refuse were similar to the pmoA gene of Methylobacter, Methylocaldum, and Methylocystis, and two clones were distinct
with known genera of Type I methanotrophs according to phylogenetic analysis. Aged refuse enriched with NMS was used for methane
biological oxidation and over 93% conversions were obtained. 相似文献
188.
The activities of CeO2 nanocubes calcined at different temperatures were tested for catalytic oxidation of o-xylene. Using CeO2 nanocubes as catalysts, complete catalytic oxidation of o-xylene was achieved below 210℃. The CeO2 nanomaterials were characterized by means of BET, X-ray diffraction (XRD), transmission electron microscopy (TEM), and high-resolution transmission electron microscopy (HRTEM). From the TEM images, all Ce02 nanocubes displayed cubic morphology irrespective of calcination temperature. The HRTEM images revealed that these nanocubes were enclosed by reactive {001}planes, which may contribute to the intrinsically catalytic property of o-xylene oxidation. The higher activity of Ce02 nanocubes calcined at 550℃ than those calcined at above 550℃ was attributed to their smaller crystallite size and larger surface area. The influences of reaction conditions were also studied, which found that a higher reaction temperature was necessary for complete catalytic oxidation of o-xylene at higher weight hourly space velocity (WHSV) and o-xylene concentration. 相似文献
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