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50·ENWoNMENrALPorEcrTOOFcHEMCALNDUsTRY 01年第31卷 [1 Takdastan A, Mehrdadi N, Azimi A A, et al. Investi- 泥减量系统除磷脱氮特性叮].土木建筑与环境工 gation of intermittent chlorination system in biological 程,2009,31(5):113-116 excess sludge reduction by sequencing batch reactors [8] Peng Dongcong, Bernet N, Delgenes J P, et al.Sim- Dn. Iran J Environ Health Sci Eng, 2009, 6(1):53 ultaneous organic carbon and nitrogen removal in an BR controlled at low dissolved oxygen concentration [2] He Minghe, Wei Chaohai. Performance of membrane D]. Chem Technol Biotechnol, 2001, 76(6): 553-558. bioreactor(MBR)system with sludge Fenton oxidation [19] Sun Lianpeng, Randall C W, Novak J T. The influ- ation of excess sludge production ence of sludge interchange times on the oxic Settling D]. Hazard mater,2010,176(1-3):597-601 Anoxic process []. Water Environ Res, 2010, 82(6) and uncoupler []. Environ Sci, 2007, 28(8): 1697 reduction induced by Tubifex tubifex in a recycle 1702 sludge reactor []. Biotechnology, 2007, 127(3) [4] Zheng Guanghong, Li Mengnan, Wang Lei, et al. 443-451. Feasibility of 2,4, trichlorophenol and malonic acid [21] Song Biyu, Chen Xiaofei. Effect of Aeolosoma hemp- as metabolic uncoupler for sludge reduction in the richi on excess activated sludge reduction [].Hazard sequence batch reactor r treatin astew ater Mater,2009,162(1):300-304 D]. Appl Biochem Biotechnol, 2008, 144(2):101 22] Feng Quan, Yu Anfeng, Chu Libing, et al.Perform ance study of the reduction of excess sludge and simul- 05] Abbassi B, Ullstein S, Capdeville B, et al. Minimi- taneous removal of zation of excess sludge production by increase of oxy combination of fluidized-and fixed-bed bioreactors with gen concentration in activated sludge flocs: experime different structured macroporous carriers [].Biochem tal and theoretical approach D].Water Res,2000,34 Eng,2008,39(2):344-352 (1):139 23] Rosenberger S, Witzig R, Manz W, et al. Operation 06] Zhan Zhang X of different membrane bioreactors: experimental results Studies on Effect and Corresponding Technical Charac and physiological state of the micro-organisms [] teristics of Excess sludge Reduction in Pressurized Bio- Water Sci technol,2000,41(10-11):269-277 logical Contact Oxidation Process [C].The 4th Inter- 24] Banu J R, Uan D K, Yeom I T. Nutrient removal in national Conference on Bioinformatics and biomedical an A/0-MBR reactor with sludge reduction [] Engineering, Chengdu: IEEE, 2010: 1-3 Bioresour Technol, 2009, 100(16): 3820-3824 7]胡学斌,柴宏祥,韩万玉,等.低溶解氧控制状态下污 (编辑王馨) ,·,·,·,·,···,·,,·,·,·,··,·,··,,·,·,,·,··,·,·,·,··,··,·,·,,·,·,,·,·,· 专利文摘· 高强度球形葡甘聚糖单宁复合型 的。/CN102151557A,2011-08-17 吸附材料及其制备方法 该发明公开了一种高强度球形葡甘聚糖单宁复 多孔共价三嗪聚合物在去除 合型吸附材料及其制备方法。它是将葡甘聚糖溶胀 水中芳香族化合物方面的应用 于分散剂的碱性混合溶剂中,控温20~50℃,进行 该发明公开了一种多孔共价三嗪聚合物在去除 脱乙酰基反应1~3h,过滤、洗去分散剂和过量的水中芳香族化合物方面的应用。去除水中芳香族化 碱,50~70℃干燥5~12h,获得脱乙酰基葡甘聚合物的方法为:将多孔共价三嗪聚合物于10~30℃ 糖;将脱乙酰基葡甘聚糖分散在含单宁的水溶液中,下投入pH为5.8~6.4的含有芳香族污染物的水体 吸附反应3~12h,过滤清洗,获得脱乙酰基葡甘聚中吸附20~30h。其中水体中芳香族化合物污染物的 糖吸附单宁材料;将脱乙酰基葡甘聚糖吸附单宁材质量浓度为0.5~90.0mg/’多孔共价三嗪聚合物与 料分散于质量分数20%~100%的分散剂中,加入含芳香族化合物的水的质量比为1:(1700~2300) 碱和交联剂,机械搅拌下进行交联反应3~24h,过该发明的多孔共价三嗪聚合物对芳香族化合物有良好 滤清洗,在温度50~90℃下干燥5~12h而制得的吸附效果。/CN02153186A,2011-08-17 21994-2015ChinaAcademicJournalElectronicPublishingHouse.alLrightsreservedhttp://www.cnki.net化 工 环 保 ENVIRONMENTAL PROTECTION OF CHEMICAL INDUSTRY 2011 年第 31 卷 [11] Takdastan A,Mehrdadi N,Azimi A A,et al. Investi￾gation of intermittent chlorination system in biological excess sludge reduction by sequencing batch reactors [J]. Iran J Environ Health Sci Eng,2009,6( 1) : 53 - 60. [12] He Minghe,Wei Chaohai. Performance of membrane bioreactor ( MBR) system with sludge Fenton oxidation process for minimization of excess sludge production [J]. Hazard Mater,2010,176( 1 - 3) : 597 - 601. [13] Ma Zongkai,Tian Yu,Cheng Haifei. Reduction of excess sludge production by cooperation action of Cu2+ and uncoupler[J]. Environ Sci,2007,28( 8) : 1697 - 1702. [14] Zheng Guanghong,Li Mengnan,Wang Lei,et al. Feasibility of 2,4,6-trichlorophenol and malonic acid as metabolic uncoupler for sludge reduction in the sequence batch reactor for treating organic wastewater [J]. Appl Biochem Biotechnol,2008,144( 2) : 101 - 109. [15] Abbassi B,Dullstein S,Capdeville B,et al. Minimi￾zation of excess sludge production by increase of oxy￾gen concentration in activated sludge flocs: experimen￾tal and theoretical approach[J]. Water Res,2000,34 ( 1) : 139 - 146. [16] Zhang Yong,Zhang Xianqiu,Wang Zhiliang,et al. Studies on Effect and Corresponding Technical Charac￾teristics of Excess Sludge Reduction in Pressurized Bio￾logical Contact Oxidation Process[C]. The 4th Inter￾national Conference on Bioinformatics and Biomedical Engineering,Chengdu: IEEE,2010: 1 - 3. [17] 胡学斌,柴宏祥,韩万玉,等. 低溶解氧控制状态下污 泥减量系统除磷脱氮特性[J]. 土木建筑与环境工 程,2009,31( 5) : 113 - 116. [18] Peng Dongcong,Bernet N,Delgenes J P,et al. Sim￾ultaneous organic carbon and nitrogen removal in an SBR controlled at low dissolved oxygen concentration [J]. Chem Technol Biotechnol,2001,76( 6) : 553 -558. [19] Sun Lianpeng,Randall C W,Novak J T. The influ￾ence of sludge interchange times on the Oxic-Settling￾Anoxic process[J]. Water Environ Res,2010,82( 6) : 519 - 523. [20] Huang Xia,Liang Peng, Qian Yi. Excess sludge reduction induced by Tubifex tubifex in a recycled sludge reactor[J]. Biotechnology,2007,127 ( 3 ) : 443 - 451. [21] Song Biyu,Chen Xiaofei. Effect of Aeolosoma hemp￾richi on excess activated sludge reduction[J]. Hazard Mater,2009,162( 1) : 300 - 304. [22] Feng Quan,Yu Anfeng,Chu Libing,et al. Perform￾ance study of the reduction of excess sludge and simul￾taneous removal of organic carbon and nitrogen by a combination of fluidized-and fixed-bed bioreactors with different structured macroporous carriers[J]. Biochem Eng,2008,39( 2) : 344 - 352. [23] Rosenberger S,Witzig R,Manz W,et al. Operation of different membrane bioreactors: experimental results and physiological state of the micro-organisms[J]. Water Sci Technol,2000,41( 10 - 11) : 269 - 277. [24] Banu J R,Uan D K,Yeom I T. Nutrient removal in an A2 /O-MBR reactor with sludge reduction [J]. Bioresour Technol,2009,100( 16) : 3820 - 3824. ( 编辑 王 馨 櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏櫏 ) ·专利文摘· 高强度球形葡甘聚糖单宁复合型 吸附材料及其制备方法 该发明公开了一种高强度球形葡甘聚糖单宁复 合型吸附材料及其制备方法。它是将葡甘聚糖溶胀 于分散剂的碱性混合溶剂中,控温 20 ~ 50 ℃,进行 脱乙酰基反应 1 ~ 3 h,过滤、洗去分散剂和过量的 碱,50 ~ 70 ℃ 干燥 5 ~ 12 h,获得脱乙酰基葡甘聚 糖; 将脱乙酰基葡甘聚糖分散在含单宁的水溶液中, 吸附反应 3 ~ 12 h,过滤清洗,获得脱乙酰基葡甘聚 糖吸附单宁材料; 将脱乙酰基葡甘聚糖吸附单宁材 料分散于质量分数 20% ~ 100% 的分散剂中,加入 碱和交联剂,机械搅拌下进行交联反应 3 ~ 24 h,过 滤清洗,在温度 50 ~ 90 ℃ 下干燥 5 ~ 12 h 而制得 的。/ CN102151557A,2011 - 08 - 17 多孔共价三嗪聚合物在去除 水中芳香族化合物方面的应用 该发明公开了一种多孔共价三嗪聚合物在去除 水中芳香族化合物方面的应用。去除水中芳香族化 合物的方法为: 将多孔共价三嗪聚合物于 10 ~ 30 ℃ 下投入 pH 为 5. 8 ~ 6. 4 的含有芳香族污染物的水体 中吸附20 ~30 h。其中水体中芳香族化合物污染物的 质量浓度为0. 5 ~ 90. 0 mg /L,多孔共价三嗪聚合物与 含芳香族化合物的水的质量比为 1 ∶ ( 1 700 ~ 2 300) 。 该发明的多孔共价三嗪聚合物对芳香族化合物有良好 的吸附效果。/ CN102153186A,2011 -08 -17 ·510·
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