首页 | 本学科首页   官方微博 | 高级检索  
相似文献
 共查询到18条相似文献,搜索用时 140 毫秒
1.
臭氧氧化二级出水有机物可生化性研究   总被引:15,自引:6,他引:9       下载免费PDF全文
通过臭氧氧化北京3个典型城市污水处理厂二级出水,考察臭氧对二级出水有机物可生化性的提高作用.采用批量试验方法,通过调整臭氧投加时间控制臭氧投加浓度为2、4、6、8、10 mg/L.结果表明,UV254与比紫外消光度SUVA(UV254/DOC)随臭氧投加量而降低,臭氧投加量为6 mg/L时,UV254与SUVA分别降低54.4%与56.6%以上;BOD5/COD、BDOC与BDOC/DOC分别提高30%、360%与360%以上,表明适当的臭氧投加量可提高二级出水难降解有机物的可生化性;三维荧光指纹光谱分析臭氧氧化前后二级出水中有机物的变化规律,表明该污水处理厂二级出水的荧光有机物主要为芳香族蛋白类物质和腐殖质类物质,臭氧可显著去除该类有机物.  相似文献   

2.
针对被典型化学品双酚A(BPA)与邻苯二甲酸二乙酯(DEP)污染原水的应急处理工艺进行了研究.结果表明,活性炭吸附可有效去除双酚A和DEP.拟二级动力学模型和Elovich模型较好地描述粉末活性炭对原水中BPA和DEP的吸附过程.中试条件下,50 mg/L的粉末活性炭可分别将原水中浓度约为500 μg/L的双酚A和3.3 mg/L的DEP处理达标.炭砂滤柱对2种化学品的动态吸附表明,BPA和DEP的去除率受它们初始浓度的影响较小,在滤速为5.1~15.3 m/h的范围内BPA和DEP的去除率基本不受滤速的影响.当同时采用粉末活性炭和炭砂滤柱工艺时, PAC的吸附过程是去除污染的主要阶段,炭砂滤柱可以作为粉末活性炭的有效补充保证一定的安全系数.KMnO4和Cl2均不能氧化DEP,3 mg/L的KMnO4和1.5 mg/L的Cl2可几乎完全氧化水中浓度为850 μg/L的BPA,BPA的氯化产物和KMnO4的氧化产物及其毒性有待于进一步研究. 1.5 mg/L高锰酸钾和PAC联用对去除DEP无协同作用,对去除BPA有促进作用.  相似文献   

3.
采用UV/H22/微曝气工艺对水中内分泌干扰物双酚A(BPA)的降解与矿化进行了试验研究.该工艺是在UV/H22的基础上发展起来的一种新工艺,微曝气在UV光照射下产生了一定量的O3,提高了·OH的发生率.本试验研究了UV光强、H22投加量以及pH值对BPA矿化速率的影响.结果表明,随着UV光强的增大,BPA的矿化速率呈线性增加;当H22投加量由5 mg/L增大到20 mg/L时,BPA矿化速率常数k由0.003 2上升到0.025 0;当pH为6.68时,在相同条件下BPA的矿化效果最好.在同一工况条件下,UV/H22/微曝气工艺降解BPA的速率远远大于其矿化速率,分析得出在开始反应阶段BPA首先被降解为小分子有机物,随着反应的进一步进行小分子有机物逐步被矿化为无机物.  相似文献   

4.
VUV/TiO2/O3去除水中微量硝基苯的研究   总被引:1,自引:0,他引:1       下载免费PDF全文
尹菁菁  张彭义 《环境科学》2009,30(1):134-139
采用负载在钛片上的二氧化钛(TiO2)薄膜光催化剂,以能发射185 nm真空紫外线(VUV)的紫外灯为光源,研究臭氧强化的真空紫外光催化方法(VUV/TiO2/O3)对水中微量硝基苯的去除效果.结果表明,VUV/TiO2/O3是一种有效地去除水中微量硝基苯的方法,VUV/TiO2/O3的表观一级反应速率常数比UV/TiO2/O3和VUV/O3分别高102.8%和30.8%,去离子水中50 μg/L的硝基苯反应60 s后就降低到检测限以下.VUV/TiO2/O3对硝基苯的降解速率随臭氧投加量的增加而显著增大,臭氧投加量1.52  mg/L时的反应速率比不加臭氧时提高了134.4%;虽然表观一级反应速率常数随初始浓度增加而稍有下降,但初始浓度170 μg/L的硝基苯反应2 min后也无法检出.水中常见的重碳酸盐和腐殖酸对硝基苯降解有显著的抑制作用,两者浓度分别为2 mmol/L和3.2  mg/L时,VUV/TiO2/O3对硝基苯的表观反应速率常数分别下降82.9%和71.6%,反应速率常数的倒数与重碳酸氢根浓度线性相关.VUV/TiO2/O3能快速有效地去除地表水(含碳酸盐和天然有机物)中的微量硝基苯,4 min内初始浓度为90 μg/L的硝基苯去除率达到96%,UV254降低了80%.  相似文献   

5.
研究了臭氧氧化对城市污水二级处理出水中15种典型药品和个人护理品(PPCPs)的去除效果及O3分子氧化和·OH自由基氧化的贡献.结果表明,PPCPs的臭氧氧化去除效果与其亲核官能结构特性相关,芳香胺结构为主的PPCPs易降解,烷基胺结构为主的PPCPs可部分降解,亲核特性较弱的双键为主的PPCPs难降解;在臭氧投加量为5.5 mg·L-1条件下,这3类PPCPs的去除率为分别为大于95%、57%~68%和39%~57%.臭氧氧化过程中,O3分子氧化和·OH自由基氧化均起重要作用.易降解PPCPs的氧化机制以O3分子氧化为主,贡献率为82%~91%;可降解和难降解PPCPs的氧化机制以·OH自由基氧化为主,贡献率分别为48%~71%和66%~94%.二级出水中臭氧氧化过程中,UVA254去除率可呈单线性或分段线性指示PPCPs的去除效率.  相似文献   

6.
伍海辉  高乃云  贺道红  徐斌  芮旻  赵建夫 《环境科学》2006,27(10):2035-2039
通过臭氧生物活性炭和微曝气生物活性炭(O3/BAC和micro-aeration/BAC)2套工艺研究其对不同相对分子质量有机物去除特点和不同相对分子量有机物生成的卤乙酸及其去除特性.结果表明,O3/BAC工艺对相对分子质量区间>30×103的有机物去除率超过90%.O3/BAC与micro-aeration/BAC出水中,UV254值表示相对分子质量<103的有机物超过50%,相对分子量区间在10×103~30×103的有机物占20%~30%;在O3/BAC和微曝气/BAC工艺出水中,以相对分子质量<103的有机物生成的卤乙酸最多,生成DCAA、TCAA、DBAA分别为97.00、38.55、2.10μg/L和104.00、42.75和2.92μg/L;采用各处理单元不同分子量有机物与氯反应生成的DCAA、TCAA、DBAA和THAAs与相对应的UV254值进行线性拟合,相关系数分别为0.827、0.851 3、0.815 7和0.878.UV254与臭氧生物活性炭处理工艺出水中的卤乙酸生成潜能具有较好的线性关系.  相似文献   

7.
铁改性掺氮碳纤维活化过一硫酸盐降解双酚A   总被引:2,自引:2,他引:0       下载免费PDF全文
通过静电纺丝制备了Fe和N掺杂改性的碳纳米纤维(Fe-N-CNF),研究了该催化剂活化过一硫酸盐(PMS)降解双酚A(BPA)的性能.以聚丙烯腈为前驱体通过添加FeCl3、尿素、NH4Cl、均苯四甲酸二酐等配制溶胶进行静电纺丝,预氧化并高温碳化后获得Fe-N-CNF,研究了Fe-N-CNF投加量、PMS投加量、溶液初始pH对BPA降解效果的影响.结果表明,当Fe-N-CNF投加量为1 g·L-1,PMS投加量为2 mmol·L-1,初始pH为5时,30 min内对初始浓度为20 mg·L-1 BPA的降解率可达100%.自由基淬灭实验和电子自旋共振波谱(ESR)分析证明,该体系中起主要作用的活性氧物种是O2·-1O2.同时研究了Fe-N-CNF/PMS体系对多种有机污染物的降解效果.  相似文献   

8.
孙志忠  赵雷  马军 《环境科学》2006,27(2):285-289
考察了水中本底成分对催化臭氧化分解水中微量硝基苯的影响规律.对比试验结果表明,单独臭氧氧化、臭氧/蜂窝陶瓷催化氧化和臭氧/改性蜂窝陶瓷催化氧化工艺在自来水中比蒸馏水中对硝基苯的去除率分别增加了4.90%、2.47%和5.12%.单独臭氧氧化对硝基苯的分解效率随着镁离子浓度的升高(0~8 mg.L-1)而增加了6.25%,在相同实验条件下,臭氧/蜂窝陶瓷催化氧化和臭氧/改性蜂窝陶瓷催化氧化对硝基苯的降解效率随着镁离子浓度的升高却降低了11.41%和17.64%;单独臭氧氧化、臭氧/蜂窝陶瓷催化氧化和臭氧/改性蜂窝陶瓷催化氧化在氯离子浓度增加(0~40 mg.L-1)的情况下对硝基苯的去除率分别下降了4.42%、9.38%和12.24%;低浓度的腐殖酸促进了硝基苯的降解,高浓度的腐殖酸抑制了硝基苯的降解.实验还研究了臭氧投加量和硝基苯初始浓度对硝基苯降解效率的影响.  相似文献   

9.
O3/H2O2去除水中硝基苯效果与机理   总被引:3,自引:4,他引:3  
以硝基苯为目标反应物,对O3/H2O2体系氧化去除水中硝基苯的效果和机理进行了研究,考察了pH值、H2O2剂量、自由基抑制剂或促进剂对硝基苯的去除效果的影响.研究发现,在pH≤7时,H2O2促进臭氧化去除硝基苯的效果较为明显,当H2O2投加量从1.0 mg/L增加到4.0 mg/L时,在氧化5 min内,硝基苯  相似文献   

10.
太阳光/硫掺杂TiO2体系对双酚A的氧化性能研究   总被引:1,自引:0,他引:1  
利用小试试验研究了太阳光和硫(S)掺杂TiO2体系对水中双酚A(BPA)的降解效能及影响因素.结果表明,太阳光/S掺杂TiO2体系对纯水中BPA的去除效能较太阳光/TiO2体系显著提高,30 min时的去除率分别为79%和49%,且两体系对BPA的降解过程均很好地符合拟一级反应动力学模型;H2O2的投加量对两体系氧化BPA的性能均有显著的影响,但其最佳投加量不同(两体系的最佳H2O2浓度分别为20 mg/L和15 mg/L,太阳光/S掺杂TiO2比太阳光/TiO2体系高5 mg/L);较低的pH值有利于两体系中BPA的降解,pH为5.5时的反应速率常数比pH为8.5时高50%左右;腐殖酸会不同程度的降低两体系对BPA的降解速率,其影响均可以用二次方程来表示.此外,腐殖酸对太阳光/S掺杂TiO2体系的弱化作用要明显强于对太阳光/TiO2体系的,原因在于腐殖酸不仅会与BPA分子竞争.OH,而且会吸收部分可激发TiO2产生.OH的可见光.  相似文献   

11.
The ozone oxidation of endocrine disruptor bisphenol A in drinking water was investigated. A stainless completely mixed reactor was employed to carry out the degradation experiments by means of a batch model. With an initial concentration of 11.0 mg/L, the removal efficiencies of BPA (bisphenol A) could be measured up to 70%, 82%, and 90% when the dosages of ozone were 1, 1.5, and 2 mg/L, respectively. The impacts on BPA degradation under the conditions of different ozone dosages, water background values, BPA initial concentrations, and ozone adding time were analyzed. The results showed that ozone dosage plays a dominant role during the process of BPA degradation, while the impact of the contact time could be ignored. UV wavelength scanning was used to confirm that the by-products were produced, which could be absorbed at UV254. The value of UV254 was observed to have changed during the ozonation process. Based on the change of UV254, it could be concluded that BPA is not completely degraded at low ozone dosage, while shorter adding time of total ozone dosage, high ozone dosage, and improvement of dissolved ozone concentration greatly contribute to the extent of BPA degradation. The effects of applied H2O2 dose in ozone oxidation of BPA were also examined in this study. The O3-H2O2 processes proved to have similar effects on the degradation of BPA by ozone oxidation. Translated from Environmental Science, 2006, 27(2): 294–299 [译自: 环境科学]  相似文献   

12.
Ozonation has been widely applied in advanced wastewater treatment. In this study, the effect of ozonation on assimilable organic carbon (AOC) levels in secondary effluents was investigated, and AOC variation of different molecular weight (MW) organic components was analyzed. Although the removal efflciencies were 47%-76% and 94%-100% for UV2s4 and color at ozone dosage of 10 mg/L, dissolved organic carbon (DOC) in secondary effluents was hardly removed by ozonation. The AOC levels increased by 70%-780% at an ozone dosage range of 1-10 mg/L. AOC increased significantly in the instantaneous ozone demand phase, and the increase in AOC was correlated to the decrease in UV254 during ozonation. The results of MW distribution showed that, ozonation led to the transformation of larger molecules into smaller ones, but the increase in low MW (〈1 kDa) fraction did not contribute much to AOC production. The change of high MW (〉100 kDa and 10-100 kDa) fractions itself during ozonation was the main reason for the increase of AOC levels. Furthermore, the oxidation of organic matters with high MWs (〉 100 kDa and 10-100 kDa) resulted in more AOC production than those with low MWs (1-10 kDa and 〈1 kDa). The results indicated that removing large molecules in secondary effluents could limit the increase of AOC during ozonation.  相似文献   

13.
使用单级和两级串联臭氧-生物活性炭(O3-BAC)处理垃圾焚烧渗滤液的二级生物处理尾水,比较研究了污染物去除效果.结果表明,臭氧投加量为200 mg·L-1时,两级串联O3-BAC对COD、UV254和色度的去除率分别为75.9%±2.1%、78.8%±2.9%和96.8%±0.9%,处理出水COD基本保持在100 mg·L-1以下,色度低于40倍,满足GB 16889-2008排放要求;而单级O3-BAC对COD、UV254和色度的去除率分别为68.2%±1.3%、69.7%±0.5%和92.5%±1.1%,处理出水COD和色度分别为150 mg·L-1和60倍,不能达到排放要求.单级O3-BAC在290 mg·L-1臭氧投加量下,才能达到两级串联O3-BAC在200mg·L-1臭氧投加量下的污染物去除效果.此外,两级串联O3-BAC在臭氧投加量200 mg·L-1时的总磷去除率为63.5%±4.4%,出水总磷浓度稳定在1 mg·L-1以下,直接满足GB 16889-2008排放要求.  相似文献   

14.
VUV/US耦合深度处理印染废水尾水的研究   总被引:1,自引:1,他引:0       下载免费PDF全文
采用真空紫外(VUV)/高频超声(US)耦合深度处理印染废水尾水,以TOC和UV254为污染物指标,比较了不同功率下VUV、US和VUV/US降解印染废水尾水的效果,以确定VUV/US的最佳功率组合;通过批式实验,探讨了反应时间、反应温度、初始pH值对VUV/US降解印染废水尾水效能的影响规律,解释了VUV/US对TOC和UV254的降解动力学.通过分析降解产物,揭示了VUV/US对印染废水尾水中残余难降解有机物的去除机理.结果表明,VUV/US的最佳功率组合为VUV16W、US100W,VUV/US处理印染废水尾水的效果明显优于单独UV和US的情况,存在着协同增效作用,反应120 min后VUV/US对TOC及UV254的去除率分别达到27.68%和93.03%.反应温度、初值pH值对VUV/US处理效果的影响较小.VUV/US降解TOC和UV254的反应动力学分别符合表观二级动力学模型和表观一级动力学模型.VUV/US过程是VUV直接光解、超声空化气泡内的热裂解和羟基自由基的氧化等协同作用,印染废水尾水中以苯系物为代表的难降解物主要通过羟基自由基的氧化作用去除.  相似文献   

15.
刘延湘  张旭  吴峰  邓南圣 《环境科学》2008,29(3):638-642
环糊精口α-CD、β-CD和γ-CD能分别与双酚A形成1:1主-客体包结物.在250W金属卤化物灯(λ≥365 nm)光照下,研究了在Fe(Ⅲ)-OH配合物体系中,不同环糊精对双酚A光降解的影响.结果表明,β-CD能较大地促进双酚A的光降解,α-CD次之,而γ-CD对双酚A的光降解存在一定的抑制;并且CDs浓度的变化对双酚A光降解的初始速率有明显的影响.双酚A光降解的初始速率随着β-CD和α-CD浓度增大而增加,当β-CD=60μmol/L时达到最大,然后随着浓度增大而降低,而BPA的光降解初始速率随γ-CD浓度的增加总的趋势是减小的.通过计算机软件Gaussian98,采用PM3方法模拟了环糊精与双酚A的包结行为,进一步说明3种环糊精与双酚A形成主-客体包结物对光降解的影响.  相似文献   

16.
UV254nm+185nm光照降解气态甲苯的实验研究   总被引:1,自引:0,他引:1       下载免费PDF全文
研究了波长为254nm+185nm紫外光照射下,甲苯初始浓度、停留时间、相对湿度、O2浓度等因素对甲苯光降解效率的影响.通过定量UV254nm+185nm光照下体系中O3的产生浓度变化,以及降解过程中中间产物苯和苯甲醛的变化趋势,讨论了甲苯在UV254nm+185nm照射下降解机理.结果表明,甲苯去除率随着O2含量、停留时间的增加而升高;随着初始浓度的增加而降低.与湿度的关系为先急剧升高然后缓慢增加,而后降低,最佳相对湿度在40%~50%.当甲苯初始浓度为16.1mg/m3,O2含量为20%,相对湿度为40%时,体系对甲苯的降解效率为82.2%,降解速率为0.44mg/(m3·s),产生的O3浓度为131.13mg/m3,中间产物苯和苯甲醛的浓度分别为0.086,0.135mg/m3.在反应体系中,甲苯可吸收185nm波长紫外光直接降解,但主要被体系中产生的自由基氧化降解.  相似文献   

17.
A three-dimensional electrochemical oxidation(3D-EC) reactor with introduction of activated carbon(AC) as particle micro-electrodes was applied for the advanced treatment of secondary wastewater effluent of a wet-spun acrylic fiber manufacturing plant. Under the optimized conditions(current density of 500 A/m~2, circulation rate of 5 mL/min, AC dosage of 50 g, and chloride concentration of 1.0 g/L), the average removal efficiencies of chemical oxygen demand(COD_(cr)), NH3–N, total organic carbon(TOC), and ultraviolet absorption at 254 nm(UV_(254)) of the 3D-EC reactor were 64.5%, 60.8%, 46.4%, and 64.8%, respectively; while the corresponding effluent concentrations of COD_(cr), NH_3–N, TOC, and UV_(254) were 76.6, 20.1, and42.5 mg/L, and 0.08 Abs/cm, respectively. The effluent concentration of COD_(cr) was less than 100 mg/L, which showed that the treated wastewater satisfied the demand of the integrated wastewater discharge standard(GB 8978-1996). The 3D-EC process remarkably improved the treatment efficiencies with synergistic effects for COD_(cr), NH_3–N, TOC, and UV_(254) during the stable stage of 44.5%, 38.8%, 27.2%, and 10.9%, respectively, as compared with the sum of the efficiencies of a two-dimensional electrochemical oxidation(2D-EC) reactor and an AC adsorption process, which was ascribed to the numerous micro-electrodes of AC in the 3D-EC reactor. Gas chromatography mass spectrometry(GC–MS) analysis revealed that electrochemical treatment did not generate more toxic organics, and it was proved that the increase in acute biotoxicity was caused primarily by the production of free chlorine.  相似文献   

18.
The source water in one forest region of the Northeast China had very high natural organic matter (NOM) concentration and heavy color during snowmelt period. The efficiency of five combined treatment processes was compared to address the high concentration of NOM and the mechanisms were also analyzed. Conventional treatment can hardly remove dissolved organic carbon (DOC) in the source water. KMnO4 pre-oxidization could improve the DOC removal to 22.0%. Post activated carbon adsorption improved the DOC removal of conventional treatment to 28.8%. The non-sufficient NOM removal could be attributed to the dominance of large molecular weight organic matters in raw water, which cannot be adsorbed by the micropore upon activated carbon. O3 + activated carbon treatment are another available technology for eliminating the color and UV254 in water. However, its performance of DOC removal was only 36.4%, which could not satisfy the requirement for organicmatter. The limited ozone dosage is not sufficient to mineralize the high concentration of NOM. Magnetic ion-exchange resin combined with conventional treatment could remove 96.2% of color, 96.0% of UV254 and 87.1% of DOC, enabling effluents to meet the drinking water quality standard. The high removal efficiency could be explained by the negative charge on the surface of NOM which benefits the static adsorption of NOM on the anion exchange resin. The results indicated that magnetic ion-exchange resin combined with conventional treatment is the best available technology to remove high concentration of NOM.  相似文献   

设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号