生活污水处理过程中最佳絮凝微生物的筛选及其生物学特性研究
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摘要
微生物絮凝剂是一类由微生物产生的具有絮凝能力的代谢产物,主要有糖蛋白、多糖、蛋白质、纤维素和DNA等。相比无机絮凝剂铝盐的易发生老年痴呆,铁盐对设备的高要求,以及丙烯酰胺单体的毒性,高效、无毒、无二次污染、可生物降解等特点使得微生物絮凝剂在水处理、食品工业等方面具有广阔的应用前景,越来越受到研究者的重视。
     1.本文考察了呼和浩特辛辛板污水处理厂处理污水过程中各阶段出水的微生物类群数量变化情况。各阶段微生物数量变化从多到少依次为活性污泥>曝气池>进水池>出水池>沉淀池。细菌、放线菌和真菌三大类微生物当中,各阶段出水都是细菌数量占绝对优势。
     2.从污水处理厂的各处理阶段出水及活性污泥中初筛得到10株絮凝活性较高的菌株。复筛后选择了两株絮凝能力最强的菌株做了进一步研究。将它们命名为X-1和X-2。经生理生化特性研究和16SrDNA序列测定,确定菌株X-1和X-2都是克雷伯氏菌属(Klebsiella sp.)的细菌。
     3.X-1的培养条件为葡萄糖20g/L,牛肉膏0.5g/L,磷酸氢二钾5g/L,磷酸二氢钾2g/L,氯化钠0.1g/L,硫酸镁为0.05g//L,硝酸钾0.2g/L培养基初始pH值7.5,培养温度30℃,摇床转速160r/m。
     菌株X-2的培养条件为葡萄糖15g/L,酵母膏1.0g/L,磷酸氢二钾为3g/L,磷酸二氢钾为2g/L,硫酸镁0.2g/L,氯化钠0.1g/L,氯化亚铁0.1g/L。培养基初始pH值7.5,培养温度30℃,摇床转速160r/m。
     4.研究了X-1和X-2两菌株的部分生物学特性。X-1和X-2都是革兰氏阴性菌,菌株X-1菌体杆状,长2μm,宽1μm。菌落直径约3mm,圆形,边缘整齐,凸起,表面光滑,半透明,乳黄色,有光泽。有荚膜,无芽孢。在X-1的生长周期中,絮凝率最高的时期是在稳定期的后期,即培养32h时。
     菌株X-2菌体长1.8μm,宽0.8μm。菌落直径3-5mm,圆形,边缘整齐,凸起,扁圆锥状,表面光滑,半透明,黄色,有光泽。有荚膜,无芽孢。X-2的生长周期中,絮凝率最高的时期是在对数生长期,即培养6h时。
     5.在100mL 0.5%的高岭土悬液体系中,pH值为8,温度为25℃,加入800μL 10%的CaCl2溶液为助凝剂,培养32h的X-1发酵液600μL150r/m快搅1min后,50r/m慢搅2min,静置30min,菌株X-1能发挥最高絮凝活性,絮凝率达到93.57%。
     对于菌株X-2来说,高岭土悬液pH值为7时,反应温度为25℃,助凝剂10%的CaCl2溶液600μL,培养6h的X-2发酵液用量500μL,搅拌方式与X-1相同等条件下,X-2絮凝率最高,达到92.82%。
     同时加入培养适宜时间的X-1和X-2的发酵液,测得的絮凝率比单一菌株作用下的絮凝率高。
     6.离心后发现X-1和X-2的絮凝活性物质都分布在上清液中。它们的热稳定性都比较高,随着温度的上升,絮凝率下降幅度不大。菌株传代次数和菌种的保存时间对两菌株的絮凝率有一定的影响。传代次数越多,絮凝活性越低。菌种保存时间越长,絮凝率也越低。
     7.在净化实际生活污水的过程中发现,在X-1和X-2两菌株共同作用下对污水的净化程度较高。
Bioflocculant is a kind of biological metabolic substance produced by microorganism which has the ability of flocculating. Its main components are glycoprotein, amylum, protein, cellulose, DNA etc. Bioflocculant is efficient, nontoxic, biodegradable readily and without pollution to the environment. The studies of bioflocculants are gaining more and more attentions.
     1. We detected the change of microbe quantity of sewage basin, aeration basin, sewage preliminary basin, sewage effluent and activated sludge in Hohhot sewage disposal plant. Microbe quantity was activated sludge, aeration basin, sewage basin, sewage effluent, sewage preliminary basin from more to less. Bacterium is dominant in Microorganism.
     2. We selected 10 strains with high flocculating activity from Hohhot sewage disposal plant.Two strains of them with higher flocculating activity were do further research and named as X-1 and X-2. X-1 and X-2 were considered as Klebsiella sp. by assaying physiological and biochemical characteristics and 16SrDN A sequence.
     3. Glucose was the best carbon source of X-1 and X-2, X-1 was 20g/L and X-2 was 15g/L. Beef extract was the best nitrogen source of X-1, when 0.5g/L it had the highest flocculating activity. Other optimum cultural conditions of X-1 were:K2HPO4 5g/L, KH2PO4 2g/L, NaCl 0.1g/L, MgSO4 0.05g/L, KNO3 0.2g/L.The initial pH value of the medium was adjusted to 7.5, and the strain X-1 was cultured at 30℃and shaken at 160 r/m in a rotary shaker for 32 hours.
     Yeast extract was the best nitrogen source of X-2, the best dosage was 1.0g/L.Other optimum cultural conditions of the strain X-2 were:K2HPO4 3g,KH2PO4 2g,NaCl 0.1g, MgSO4 0.2g, FeCl2 0.1g in 1000mL distilled water. The best condition for X-2 were:the initial pH was 7.5, Temperature was 30℃, and shaken at 160 r/m in a rotary shaker for 6 hours.
     4. We studied some biological characteristics of the two strains. X-1 and X-2 were gram-negative bacteria.
     In the X-1's growth cycle, the highest rate of flocculation appeared in stable phase,32h cultured. In the X-2 growth cycle, the highest rate of flocculation appeared in logarithmic phase, that is, when cultured 6h.
     5. X-1 could play the highest flocculating activity and its flocculating rate was 93.57%, when 0.5% kaolin suspension system in 100mL. And pH was 8, the temperature was 25℃, to add 800μL 10% CaCl2 as coagulant,32h cultured of the 600μL X-1 fermenting liquor,150r/m lmin,50r/m 2min, standing for 30min.
     When pH of the kaolin suspension was 7, the reaction temperature was 25℃,10% CaCl2 was 600μL, the amount of X-2 liquid was 500μL 6h cultured, stirring the same way as X-1 for the X-2, flocculation rate of X-2 was to 92.82%,that was the highest flocculation rate of X-2.
     6. After centrifugation, we found that the flocculating activity of substances of X-1 and X-2 both mainly existed in the supernatant. The flocculants produced by X-1 and X-2 relatively had high thermal stability, as the temperature increased the flocculation rate decreased slightly. To a certain extent, times of bacteria passages and storage time had effect on the flocculation rate. The more passages bacteria were, the lower flocculating activity was. The longer preservation species was, the lower flocculation rate was.
     7. We found that X-1 and X-2 acted on sewage together, sewage disposal consequence was better than X-1 or X-2 acted alone.
引文
[1]Klaus-Dieter Balke,朱琰.水与发展[M].北京:地质出版社,2003:170-173.
    [2]王瑾.絮凝剂在废水处理中的应用及絮凝体沉降动力学研究[D].天津:天津轻工业学院,2000:
    [3]常青.水处理絮凝学[M].北京:化学工业出版社,2003:1-2.
    [4]田玲,王思九,李玉金.水处理絮凝剂的絮凝原理及其研究进展[J].自然科学学报,2004,18(1):54-57.
    [5]苏林.絮凝淤泥中絮凝剂降解的初步研究[D].南京:南京理工大学,2008:
    [6]徐国想,阮复昌.铁系和铝系无机絮凝剂的性能分析[J].重庆环境科学,2001,23(3):52-55.
    [7]崔蕴霞.铝盐絮凝剂及其环境效应[J].工业水处理,1998,18(3):6-9.
    [8]郑怀礼,龙腾锐,舒型武.聚合铁类絮凝剂絮凝作用机理分析[J].重庆环境科学,2000,22(5):51-53.
    [9]崔小明.微生物絮凝剂[J].化工纵横,1997,11(3):13-15.
    [10]永泽满,潼泽章.高分子水处理技术[M].陈振兴,tran. Beijing:Chemical Industry Press, 1985:21-32.
    [11]Levy N., Magdasi S., Bar-Or Y.. Physico-chemical Aspects in Flocculation of Bentonite Suspensions by a Cyanobacterial[J]. Water Res,1992,26:249-254.
    [12]郑怀礼.生物絮凝剂与絮凝技术[M].北京:化学工业出版社,2004:47-49.
    [13]常玉广,马放,工博等.高效絮凝菌的鉴定及絮凝特性研究[J].哈尔滨工业大学学报,2010,42(10):1609-1613.
    [14]王卫平,朱凤香,陈晓旸等.微生物絮凝剂的研究进展及其应用前景[J].安徽农学通报,2009,15(19):45-48.
    [15]龙文芳,李小明,曾光明.生物絮凝剂在废水处理中的研究进展[J].净水技术,2004,23(2):25-27.
    [16]Fujita Masanori,Hiroki Takagi. Characterization of a Bioflocculant Produced by Citrobacter sp. TKF04 from Acetic and Prop ionic Acids[J]. Bioscience Bioengineering,2000,89(1):40-46.
    [17]Zajic J E, Knetting Eva. Developments in Industrial Microbiology[M]Washington D C.:American Institute of Biological Science,1971:87-98.
    [18]Nakamura J., et al. Purification and Chemical Analysis of Microbial Cell Flocculants Produced by Aspergillus Sojae AJ7002[J]. Agric Biol Chem,1976,40(3):619-624.
    [19]Nakamura J., Miyashiro S., Hirose Y. Screening Isolation and Some Properties of Microbial Cell Flocculants[J]. Agric. Biol. Chem.,1976,40(2):377-383.
    [20]Takagi H., Hadowaki K.. Flocculant Production by Paecilomyces sp. TaXonomic Studies and Culture Conditions for Product ion[J]. Agric. Biol. Chem.,1985,49(11):3151-3157.
    [21]Shimiziu N. Floc-forming Bacteria Isolated from Activated Sludge in High BOD Loading Treatment[J]. Ferment Technol,1985,63:67-71.
    [22]Kurane R., NohataY. Microbail Flocculation of Wastewater Liquid and Oil Emulsion by a Bioflocculant from Alcaligenes Latus[J]. Agric Biol Chem,1991,55(4):1127-1129.
    [23]Takeda M.,Kurane J. Localization of a Biopolymer Produced by Rhodococcus Erythropolis, Grown on n-pentadecane[J]. Agri. Biol. Chem.,1991,55(10):2663-2664.
    [24]张沫.高效微生物絮凝菌的筛选及其特性研究[D].哈尔滨:哈尔滨工业大学,2006:
    [25]Suh H. H., Kwon G. S., Lee C. H. et al. Characterization of Bioflocculant Produced by Bacillus sp. DP-152[J]. Journal of Fermentation and Bioengineering,1997,84(2):108-112.
    [26]Suh H. H., Moon S. H., Kim H. S., et al. Production and Rheological Properties of Bioflocculant Produced by Bacillus sp. DP-152[J]. Journal of Microbiology and Biotechnology,1998,8(6):618-624.
    [27]Suh H. H., Moon S. H., Seo W. T., et al. Physico-chemical and Rheological Properties of a Bioflocculant BF-56 from Bacillus sp. A56[J]. Journal of Microbiology and Biotechnology,2002,12(2):209-216.
    [28]Wanabe M., et al. Flocculation Property of Extracellular Polymeric Substance Derived from Marine Photosyn Thetic Bacterium Rhodovulun sp. [J].Journal of Bioscience and Bioenineering,1999,87(5):625-629.
    [29]Shih I. L., etal. Production of a Biopolymer Flcculants from Bacillus Licheniformis and Its Flocculation Properties[J]. Bioresource Technology,2001,78(03):267-272.
    [30]C. GaneshKumar, Han-Seungjoo, Jang-WonChoi, et al. Purification and Characterization of an EXtracellular Polysaccharide From Haloalkalophilic Bacillus sp.Ⅰ-450[J]. Enzyme and Microbial Technology,2004,34:673-681.
    [31]张本兰.新型高效、无毒水处理剂——微生物絮凝剂德开发与应用[J].工业水处理,1996,16(1):7-8.
    [32]李智良,张本兰,裴键.微生物絮凝剂产生菌的筛选及相关废水絮凝效果试验[J].应用与环 境生物学报,1997,3(1):67-70.
    [33]邓述波,余刚,蒋展鹏等.微生物絮凝剂MBFA9的絮凝机理研究[J].水处理技术,2001,2(1):22-25.
    [34]邓述波,胡筱敏,罗茜.高效生物絮凝剂的培养条件及特性[J].东北大学学报,1999,20(5):525-528.
    [35]马放,刘俊良,李淑更等.复合型微生物絮凝剂的开发[J].中国给水排水,2003,1(19):4-7.
    [36]方明中.复合型微生物絮凝剂制备即絮凝性能的研究[D].广州:广东工业大学,2008:
    [37]马放,冯玉杰,任南琪.环境生物技术[M].北京:化学工业出版社,2003:150-153.
    [38]卫扬保,微生物生理学[M].北京:高等教育出版社,1989:18-38.
    [39]朱超英,马荣骏,何静.微生物絮凝剂及其研究与应用综述[J].矿冶工程,2003,23(4):19-22.
    [40]Kurane R, Takeda K, Suzuki T. Screening for and Characteristics of Microbial Flocculants[J].Agric Biol Chem,1986,50(9):2301-2313.
    [41]徐美娟,易贤辉.制浆造纸废水的微生物絮凝剂[J].环境保护,2003,5:53-56.
    [42]马放,杨基先,金文标等.环境生物制剂的开发与应用[M].北京:化学工业出版社,2004:211.
    [43]刘杨.产絮菌的分离鉴定及絮凝成分分析[D].哈尔滨:黑龙江大学,2008:
    [44]Richard F. Unz, Samule R Farrah. EXoploymer Production and Flocculation by Zoogloea MP6. [J]. Appl Environ Microbial,1976,31(4):623-626.
    [45]Jarkko Hantuta, Dennis H. Bamford. The Efficiency of the Protein-dependent Flocculation of Flavobacterium sp. is Sensitive to the Composition of Grown Medium. [J].Appl Microbiol Biotechnol,1991,36:100-104.
    [46]Endo T., Nakamura K.,Takahashi H. Pronase-susceptiple Floc-forming Bacteria: Relationship between Flocculation and Calciumion[J]. Agri Biol Chem,1995,40:2289-2295.
    [47]Chen S. Flocculation of Mineral Fines Using by Hydrophobic Mycobacterium phlei. Waste Process Recycl Min Metall[J]. Ind Pro Int Symp,1992,483-491.
    [48]Misra M. Selective Flocculation of Fine Coal with Hydrophobic Mycobacterium phlei. [J]. Miner Metall Process,1992,10(1):20-23.
    [49]Yokoya Fumio. Flocculation of Yeast Cells by Lactobacillus fermentum. [J]. Rew Microbiol,1991,22(1):12-16.
    [50]秦培勇,张通,陈翠仙.微生物絮凝剂MBFTRJ21的絮凝机理[J].环境科学2004,25(3):69-72.
    [51]Hiroaki Takagi. Purification and Chemical Properties of a Flocculant Produced by Paecilomices sp. [J].Agri Biol Chem,1985,49(11):3159-3164.
    [52]王友政,扬桂文,丛潇等.渔用微生物絮凝剂产生菌的筛选及培养条件研究[J].齐鲁渔业,2007,24(12):33-36.
    [53]彭晓文,邱廷省,陈明.微生物絮凝剂的絮凝特性及废水处理研究[J].皮革科学与工程,2004,14(1):43-46.
    [54]彭晓文,邱廷省,陈明.微生物絮凝剂产生菌的初步筛选及条件试验[J].安全与环境学报,2004,4(3):62-64.
    [55]杨贵生,尹华,彭辉等.微生物絮凝剂的研制及其对浊度去除的研究[J].环境科学与技术,2004,27(2)10-16.
    [56]成文,胡勇有.四种微生物絮凝剂特性的研究[J].精细化工,2004,21(2):141-143.
    [57]成文,胡勇有.四种微生物絮凝剂的相对分子量及化学组成[J].环境化学,2004,23(2):227-228.
    [58]Salehizadeh H.,Vossoughi M., Alenzadeh I.Some Investigations on Bio-flocculant Producing Bacteria[J].Biochemical Engineering Journal,2000,5:39-44.
    [59]Salehizadeh H.,Shojaosadatis A. EXtracellu-lar Biopolymeric Flocculants Recent Trends and Biotechnological Importance Biotechnology Advances[J]. Biotechnology advances,2001,19:371-385.
    [60]张艳.青海絮凝产生菌生物学特性及絮凝效应的研究[D].西宁:青海师范大学,2008:
    [61]Butterf ield CT. A Zoogloea-Forming Bacteria Isolated from Activated Sludge, Stuidies of Sewage Purification[M]. Public Health Rep,1935,50:671-681.
    [62]马青山,贾瑟,孙丽眠等.絮凝化学和絮凝剂[M].北京:中国环境科学出版社,1990:49-57.
    [63]Sakka K., Takahashi. DNA as a Flocculation Factor in Pseudomonas sp. [J].Agri Biol Chem,1981,45(2):2869-2876.
    [64]张彤,朱怀兰,林哲.微生物絮凝剂的研究与应用进展[J].应用与环境生物学报,1996,2(1):95-105.
    [65]有马咎,田村学造.郭丽华,任玉龄译.生物技术净化环境[M].北京:化学工业出版社,1990:73-79.
    [66]刘志勇.微生物絮凝泥煤水的试验及絮凝机理研究[D].淮南:安徽理工大学,2009:
    [67]何宁,李寅,陆茂林等.营养和环境条件对生物絮凝剂合成的影响[J].应用与环境生物学报,2001,7(5):453-455.
    [68]李和平,郑泽根,朱柱等.微生物絮凝剂[J].重庆环境科学,2000,22(2):18-22.
    [69]陈晓肠,杨翔华,王洪媛.微生物絮凝剂菌株的筛选和絮凝活性影响因素的考察[J].水处理技术,2004,30(3):144-146.
    [70]陆柱,蔡兰坤,陈中兴等.微生物与水处理工程[M].北京:化学工业出版社,2002:139-140.
    [71]Bar-Or Y.,Shilo M.,Characterization of Macromolecular Flocculants Produced by Phormidium sp. J-1 and by Anabaenopsis circularis PCC 6720[J].Appl Environ Microbiol, 1987,53:2226-2230.
    [72]Junji Nakamura.Modes of Flocculation of Yeast Cells with Flocculant Produced by Aspergillus sojae AJ7002[J]. Agri Biol Chem,1976,40(8):1565-1571.
    [73]朱国营.微生物絮凝剂的产生条件及絮凝性能研究[D].杭州:浙江大学,2004:
    [74]程金平,张兰英,张玉玲.微生物絮凝剂的絮凝性能研究[J].吉林大学学报,2002,32(4):413-416.
    [75]李涛.聚合氯化铝与有机高分子的复合絮凝剂特性研究[D].西安:西安建筑科技大学,2004:
    [76]邱涌涛.有机高分子絮凝剂的絮凝特征及絮凝机理初探[D].北京:中国地质大学,2007:
    [77]李军,王淑莹.水科学与工程实验技术[M].北京:化学工业出版社,2002:25-27.
    [78]H. Yokoi,0. Natsuda, J. Hirose,S.Hayashi,and Y. Takasaki, Characteristics of a Biopolymer Flocculant Produced by Bacillus sp. PY-90[J]Ferment. Bioeng.,1999:82-84.
    [79]沈萍,范秀容,李广武.微生物学实验[M].北京:高等教育出版社,1999:116-123.
    [80]黄秀梨.微生物学实验指导[M].北京:高等教育出版社,1999:33-40.
    [81]黄秀梨,辛明秀.微生物学实验指导[M].北京:高等教育出版社,2008:39-50.
    [82]陶然,杨朝晖等.微生物絮凝剂产生菌的筛选、鉴定及其培养条件的优化研究[J].中国生物工程杂志,2005,25(8):76-81.
    [83]胡筱敏,邓述波,牛力东等.一株芽孢杆菌所产絮凝剂的研究[J].环境科学研究,2001,14(1):36-40.
    [84]王镇,王孔星,谢裕敏等.几株絮凝剂产生菌的特性研究[J].微生物学报,1994,35(2),121 130.
    [85]黄玉柳,吕敏.微生物絮凝剂的研究[J].安徽农业科学,2010,38(18):9409-9411.
    [86]石璐,寻立祥,刘忠义.微生物絮凝剂的絮凝特性研究[J].工业水处理,2004,24(6):26-28.
    [87]Barry T,Collgran G, Glennon M. The 16s/23s Ribosomal Spacer Region as a Target for DNA Probes to Identify Eubacteria[J]. PCR Methods APP,1991,1:51.
    [88]曲睿娟.高效微生物絮凝剂产生菌筛选及絮凝特性研究[D].太原:山西大学,2009:
    [89]R. E.Buchanan, N. E. Gibbons. Bergey's Manual of Determinative Bacteriology[M]. The Williams & Wilkins Company, Baltimore,1974:446-447.
    [90]John G.Holt. The Shorter Bergey's Manual of Determinative Bacteriology[M]. The Williams & Wilkins Company,Baltimore,1977:110-111.
    [91]Kurane R, Nohata Y. Production of an Extracellular Polysaccharide Bioflocculant by Klebsiella pneumoniae[J].Bioscience Biotechnol Biochem,1999,63(12):2064-2068.
    [92]吕向红.微生物絮凝剂[J].化工环保,1994,15:211-218.
    [93]张永奎,周礼,陈晓等.MBF-33絮凝特性研究[J].环境科学与技术,2006,29(10):37-38.

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