薛嘉,黄钧,李毅军.高负荷厌氧/好氧一体化生物反应器的运行特性.中国给水排水,2006,15(13):30-33 Xue,J.,Huang,J.,Li,Y.J. High load anaerobic/anaerobic biological reactor integration of the operation characteristic. China Water and Wastewater 2006,15(13):30-33 (in Chinese)
[2]
Li Z. D. Integrated submerged membrane bioreactor anaerobic/Aerobic (ISMBR-A/O) for nitrogen and phosphorus removal during oil refinery wastewater treatment. Petroleum Science and Technology, 2010, 28(3):286-293
[3]
Zhang B.G.,Zhao H.Z., Zhou S.G.,et al.A novel UASB-MFC-BAF integrated system for high strength molasses wastewater treatment and bioelectricity generation. Bioresource Technology, 2009, 100(23): 5687-5693
[4]
王琳.污水处理工艺一体化生物反应器的研究现状与发展.广东化工, 2010,27(5):301-303 Wang L. Sewage treatment process integration biological reactor research present situation and the development. Guangdong Chemical Industry,2010,27(5):301-303 (in Chinese)
Bortone G., Reg Emilia Romagna, Direz Gen Ambiente.Integrated anaerobic/aerobic biological treatment for intensive swine production. Bioresource Technology, 2009, 100(22):5424-5430
[7]
张奎,刘海成. 产酸脱硫反应器中COD/SO42-比对硫酸盐去除率的影响研究.科学技术与工程, 2007,(6):1120-1122 Zhang K.,Liu H.C. Acid yield desulfurization reactor COD/SO42-than the influence of sulphate removal rate. Science Technology and Engineering,2007,(6):1120-1122 (in Chinese)
[8]
王琳. 一体式UASB-MBR反应器处理高浓有机废水.中国给水排水, 2006,22(15):33-36 Wang L. Integrated UASB-MBR reactor high concentration organic wastewater treatment. China Water and Wastewater,2006,22(15):33-36 (in Chinese)
[9]
罗丹. 对高浓度硫酸盐废水厌氧处理条件控制的研究. 环境保护与循环经济, 2010,(7):52-54 Luo D. High concentrations of sulphate wastewater anaerobic treatment condition of control.Environmental Protection and Recycling Economy, 2010,(7):52-54 (in Chinese)
[10]
Woo-lk Sohn, Dong-Hyun Ryu, Sae-Joong Oh, et al. A study on the development of composite membranes for the separation of organic vapors.Journal of Membrane Science,2000,175(2):163 -170
[11]
王爱杰,任南琪,计红芳,等. 产酸脱硫反应器中影响硫酸盐还原的关键因素研究.哈尔滨工业大学学报, 2002,34(4):445-449 Wang A.J.,Ren N.Q.,Ji H.F.,et al.Study on the influence of acid yield desulfurization reactor sulfate reduction. Journal of Harbin Institute of Technology,2002,34(4):445-449 (in Chinese)
[12]
王浩源,缪应祺. 高浓度硫酸盐废水治理技术的研究.环境导报,2001,98(1):22-25 Wang H.Y.,Miu Y.Q. High concentrations of sulfate wastewater treatment technology. Environment Herald,2001,98(1):22-25 (in Chinese)
[13]
邱国华,胡龙兴.污水处理一体化装置的研究现状与展望. 环境污染治理技术与设备,2005,6(5):7-15 Qiu, G.H., Hu, L.X. Sewage treatment integration device research situation and expectation. Techniques and Equipment for Environmental Pollution Control,2005,6(5):7-15 (in Chinese)
[14]
夏世斌,刘俊新.立体循环一体化氧化沟处理城市污水研究. 中国给水排水, 2002,18 (6): 1-4 Xia, S.B.,Liu,J.X. Stereo circulation integrated oxidation ditch the urban sewage treatment. China Water and Wastewater,2002,18(6):1-4 (in Chinese)
[15]
You S.J., Damodar R.A., Hou S.C. Degradation of Reactive Black 5 dye using anaerobic/aerobic membrane bioreactor (MBR) and photochemical membrane reactor. Journal of Hazardous Materials, 2010, 177(1-3):1112-1118
[16]
梅丽,杨平,郭勇.厌氧-好氧一体化反应器固定化微生物处理茶多酚废水实验研究.四川大学学报(工程科学版), 2007,39(1):83-87 Mei,L.,Yang,P.,Guo,Y. The application of anaerobic-aerobic integration reactor immobilized microorganism tea polyphenols wastewater treatment research.Journal of Sijuan University,2007,39(1):83-87(in Chinese)
[17]
Ahmad R., Mondal P. K., Usmani S.Q.UASFB-aerobic bioreactor for biodegradation of acid yellow-36 in wastewater. Bioresource Technology, 2010, 101(10):3787-3790
[18]
Zhang D. J., Lu P. L., Long T. R., et al. The Integration of methanogensis with simultaneous nitrification and denitrification in a membrane bioreactor. Process Biochemistry, 2005,40(2):541-547
Zhao Z. Y., Jiang G.Q., Jiang S.Y., et al.Integrated anaerobic/aerobic biodegradation in an internal airlift loop reactor for phenol wastewater treatment. Korean Journal of Chemical Engineering, 2009, 26(6):1662-1667
[21]
胡勇,尚连生,刘永红,等. 厌氧颗粒污泥床反应器污泥的流失与对策.工业用水与废水, 2007,38(4):6-8 Hu Y., Shang L.S.,Liu Y.H.,et al. Anaerobic granular sludge bed reactor was the loss of the sludge, and puts forward some countermeasures. Industrial Water and Wastewater,2007,38(4):6-8 (in Chinese)
