利用工业废水生产生物絮凝剂及其性能研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
生物絮凝剂是一类由活细胞产生具有絮凝活性的代谢产物,具有絮凝范围广、对人体无毒无害、可生物降解等特点。限制生物絮凝剂应用的因素之一是成本过高。本课题的研究主要是找出廉价的培养基,制备出无危害,无二次污染的生物絮凝剂,并对其进行废水处理的应用研究。
     从空气和活性污泥中筛选出絮凝剂产生菌,对其进行筛选并纯化得到2株絮凝活性较高且稳定的菌株,命名为M-1、M-2。对M-1及M-2进行菌种初步鉴定,M-1为微球菌属,M-2为芽孢杆菌属。以啤酒废水为廉价培养基,对这两株菌的复合菌(M1-2)进行培养,考察外加碳源、氮源、培养基pH值、培养时间等因素对复合菌絮凝效果的影响。得出了M1-2的最佳培养条件:直接利用啤酒废水,无需另外添加碳源和氮源,只需添加0.5%的KH2PO4,温度为30℃,培养基初始pH值为8.5,培养时间为48h,摇床转速160rpm。在此条件下所产生的絮凝剂对高岭土悬浊液絮凝率高达95.0%,说明啤酒废水中含有丰富的营养物质,作为培养基为絮凝剂产生菌M1-2提供丰富的碳源和氮源,从而大大的降低了培养成本,由啤酒废水生产的生物絮凝剂具有较好的絮凝活性。
     利用生物絮凝剂粗品对大庆某化工厂的含油废水进行处理,通过考察水力搅拌时间、絮凝剂和助凝剂投加量以及pH值因素对絮凝效果的影响,并结合正交试验来确定最佳操作条件,通过对水质指标检验,评价絮凝剂对废水的处理效果。对于复合菌生物絮凝剂应用含油废水的实验结果表明,在pH值为9,生物絮凝剂投加量为6mL, CaCl2投加量为6mL时,其絮凝率可达90.5%,化学需氧量(COD)去除率为68.7%,氨氮去除率大于95%,表明用啤酒废水制备生物絮凝剂处理含油污水还是可行的。
Bioflocculant is one kind of metabolic product produced by the living cell, which has the flocculating activity. Its characteristics include the broad flocculating scope, non-toxic to human and biodegradable, etc. One of factors that limit bioflocculants application is the excessively high cost. The objective of this study is to look for the low-cost culture medium and prepare harmless and no secondary pollution bioflocculants. Waste water treatment application research has been carried with the bioflocculants.
     Flocculant-producing bacteria were isolated mainly from the air and activated sludge. After secondary screening, two strains that had higher and stable flocculating activity were obtained and they were named as M-1, M-2, respectively. M-1 strain was identified as Bacillus and M-2 strain was identified as Micrococcus Cohn. Brewage wastewater was used as low-cost medium to culture mixed bacterium M1-2. The influence of factors of external carbon source, nitrogen source, medium pH value, culture time etc. on strain flocculation effect was investigated and its culture conditions were optimized. The flocculating rate of kaolin suspension was up to 95.0% under the conditions as that the carbon and nitrogen sources was not needed to add, cultivating temperature 30℃, initial pH of culture medium 8.5, cultivating time 48 h and shaking speed 160 rpm, which shows that the brewery wastewater contained rich nutrient which can provide abundant carbon and nitrogen sources for flocculant-producing bacteria species M1-2 and it is feasible to take advantage of distillery wastewater to culture the mixed M1-2, so that the culture cost could be reduced greatly. The bioflocculant that produces by brewery wastewater has better flocculating activity.
     The crude flocculant performance was studied in the oil wastewater from Daqing some chemical plant. The effects of hydraulic mixing time, flocculant volume, the volume of CaCl2 solution and pH values factors on coagulation were studied. The best treatment conditions were determined by orthogonal test and some water quality index were monitored to evaluate the flocculant effect in these wastewater treatment processes. Mixed bacterium bioflocculant was studied in chemical plant. In the condition of pH value of 9, the flocculants volume of 6mL, the CaCl2 solution (1%) volume of 5mL, the flocculation rate was 90.5%, the removal rate of COD was 68.7%, and the removal ammonia-nitrogen was more than 95%. The results indicate that oil wastewater treatment with the bioflocculant is feasible.
引文
[1]国家环境保护局,混凝剂与絮凝剂[M].北京:中国环境出版社,1991,63-64.
    [2]Salehizadeh H, Vossoughi M, Alemzadeh I, Some investigations on bioflocculant producing bacteria [J]. Biochemical Engineering,2000,5:39-44.
    [3]严瑞瑄.水处理剂应用手册[M].北京:化学工业出版社,2000,25-36.
    [4]魏玉君,邱梅,朱明.絮凝剂在造纸废水中的应用与研究简介[J].纸和造纸,2008,3(27):70-72.
    [5]张瑞霞,陈夫山,刘廷志.絮凝剂在制浆造纸废水处理中的应用[J].黑龙江造纸,2005,3:42-46.
    [6]黄德丰.环境铝的生物化学毒性[J].环境科学丛刊,1990,13(3):32.
    [7]Kurane R, Takeda K, Suzuki T. Screening for and characteristic of mcrobial flocculants [J]. Agric Biol Chem,1986,50 (9):2301-2307.
    [8]Dearfield K L, Abernathy C.O., et al.Acrylamide:its metabolism, developmental and reproductive effects, genotoxicity and carcinogenicity [J]. Mutat. Res,1988,195:45-77.
    [9]张本兰.新型高效无毒水处理剂-生物絮凝剂的开发与应用[J].工业水处理,1996,16(1):7-8.
    [10]宫小燕.生物絮凝剂的研制和应用[D].中科院生态境研究中心,北京:2002.
    [11]董延茂,赵丹,沈耀良.生物絮凝剂的应用[J].污染防治技术,2002,15(2):21-23.
    [12]罗平,邹小兵,罗固源.胞外多糖生物絮凝剂RL-2的性能研究[J].水处理技术,2005,31(6):20-23.
    [13]Nakamura J, Miygeyshi S, Hirose Y. Modes of flocculantion of yeast cells with flocculants produced by Aspergillus sojae AJ7002 [J]. Agr. Biol. Chem,1976,4(8): 1565-1571.
    [14]Kurane R, Masuyama H. Production of a bioflocculant by mixed culture [J]. Biosci Biotechnol Biochem,1994,58(9):1589-1594.
    [15]Kurance R, etal. Microbial Flocculants [J]. Bio-industry,1990,7 (1):35-60.
    [16]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,2004,8(2):25-27.
    [17]Kumne R. Micmbial flocculant from Alcaligenes cupidus KT201 [J]. Agile Biol Chem, 1991,55(11):2793-2799.
    [18]Takagi H. Purification and chemical properties of a flocculant procuced by Paecilomyces [J]. Agric Biol Chem,1985,49(11):3159-3164.
    [19]Tago Y, Aida K. Exocellular mucopolysaccharide closely related to bacterial flocculant ion. Applied and Environmental Microbiology [J].1997,34(3):308-314.
    [20]Jang JH, Ike M, Kim SM et al. Production of a novel bioflocculant by fed-baculture of citrobacter sp[J]. Biotechnology Letters,2001,23(8):593-597.
    [21]张晓辉,等.生物絮凝剂的制备及在建材加工废水处理中的应用研究[J].安全与环境工程,2003,10(3):27-30.
    [22]刘杏,邵林广,张丽芳.生物絮凝剂的研究现状及发展趋势[J].孝感学院学报.2001,21(6).
    [23]辛定平.生物絮凝剂的研究和应用[J].环境科学进展,1998,6(5):57-61.
    [24]陆茂林.生物絮凝剂产生茵的筛选和发酵条件研究[J].工业生物,1997,27(2):25-28.
    [25]陆茂林,施大林等.生物絮凝剂的制备及其絮凝条件的研究[J].食品与发酵工业,1997,23(3):23-28.
    [26]李智良,张本兰,裴健.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.
    [27]庄源益,戴树桂,李彤,等.生物絮凝剂对水中染料絮凝效果探讨[J].水处理技术,1997,23(6):349-353.
    [28]宫小燕,王竞,周集体.絮凝剂产生菌的筛选及其培养条件优化[J].环境科学研究,1999,12(4):9-11.
    [29]沈荣辉,应惠芳,黄民生.微生物絮凝剂研制条件优化和废水净化研究[J].化工装备技术,2000,21(6):31-35.
    [30]黄民生,晚宇凯,朱莉.微生物絮凝剂净化废水实验研究[J].工业水处理,2000,20(5): 13-15.
    [31]胡筱敏,邓述波,牛力东,等.一株芽袍杆菌所产絮凝剂的研究[J].环境科学研究,2001,14(1):36-40.
    [32]余荣升,徐龙君.微生物絮凝剂的现状与前景分析[J].环境污染与防治,2003,25(2):77-79.
    [33]周旭,黄丽萍,王竞,周集体,张劲松.利用鱼粉废水产生生物絮凝剂及其性能研究[M].应用与环境生物报,2003,9(4):436-438.
    [34]Kurane R, Toeda K, Takeda K, et al. Sreening for and characteristics of microbial flocculants[J]. Agric. Biol. Chem,1986,50 (9):2309-2313.
    [35]王正林,冯贵颖,岳晓勤,等.絮凝剂产生菌的筛选及产生絮凝剂的影响因素研究[J].西北农林科技大学学报(自然科学版),2003,31(2):99-104.
    [36]程金平,郑敏,张兰英,等.影响微生物絮凝剂产生的因素研究[J].环境科学与技术,2001,24(3):28-31.
    [37]石璐,寻立祥,唐受印,等.高效絮凝剂产生菌的筛选、鉴定及培养条件优化[J].湘潭大学自然科学学报,2003,25(1):50-52.
    [38]戴艳华,曹同川.胞外聚合物合成与研究概况[J].环境科学与技术,2004,27(21):140-142.
    [39]李亮,董怡华,胡筱敏,等.一株絮凝剂产生菌培养条件的优化研究[J].安全与环境学报,2005,4(4):331-334.
    [40]何秀萍,郭文洁,张博润,等.絮凝基因(FLO1G)的序列测定及分析[J].生物学报,2002,42(2):242-245.
    [41]甘莉,孟召平. 生物絮凝剂的研究进展[J].水处理技术,2006,32(4):7.
    [42]王镇,王孔星,谢裕敏.几株絮凝剂产生菌的特性研究[J].微生物学报,1995,35(2): 121-129.
    [42]李兆龙.生物絮凝剂[J].上海环境科学,1991,10(9):45-46.
    [43]陈立丰,李明俊,万诗贵,等.高浊度水絮凝过程的动力学和机理研究[J].水处理技术,1996,22(3):157-161.
    [44]田春.微生物絮凝剂的絮凝机理研究[J].内蒙古科技与经济,2002,7:98-99.
    [45]Hee-Mock Oh, Seog June Lee, Myung-Hwan Park, et al. Harvesting of Chlorella vulgaris using a bioflocculant from Paenibacillus sp. Am49[J]. Biotechnology Letters,2001, 23(4):1229-1234.
    [46]邓述波,胡筱敏,罗茜.微生物絮凝剂处理淀粉废水的研究[J].工业水处理,1999,19(5): 8-10.
    [47]尹华,彭辉.生物絮凝剂产生菌筛选及其絮凝除浊性能[J].城市环境与城市生态,2000,13(1):10-12.
    [48]黄晓武,成文,胡勇有.生物絮凝剂处理建材废水研究[J].工业用水于废水,2004,35(3):25-27.
    [49]王琴,王辉,马放,等.复合型生物絮凝剂的应用研究[J].工业水处理,2007,27(4):68-71.
    [50]杨圣云,林波,李昌花,等.絮凝剂HXCS-1处理乳化液废水[J].江西科学,2006,24(2):147-149.
    [51]陈烨,等.啤酒厂废水的生物处理[J].食品科学,2004,25(10):148-150.
    [52]陶涛,卢秀清,冷静.生物絮凝剂研究与应用进展[J].环境科学进展,1999(7):21-25.
    [53]马希晨,韩铁民,谭凤芝,等.MBF生物絮凝剂的制备与应用[J].环境保护科学,2002,28(4):13-14.
    [54]张志强,林波,夏四清,等.高活性生物絮凝剂处理靛蓝印染废水的动力学研究[J].工业水处理,2007,27(4):44-47.
    [55]张本兰.新型高效、无毒水处理剂生物絮凝剂的开发与应用[J].工业水处理,1996,16(1):7-8.
    [56]周玉松,任福民,夏四清,等.化学生物絮凝工艺去除城市污水中重金属的研究 [J].中国给水排水,2006,22(5):10-18.
    [57]Toeda K, Kurane R. Microbial flocculant from Alcaligenes cupidas KT201. Agric Biol Chem 1991,55(2):2793-9.
    [58]尹华,等.生物絮凝剂JMBF-25的结构和性质[J].中国给水排水,2003,19(1):1-4.
    [59]Sub H, Kwon G, Lee C. Characterization of bioflocculant produced by Bacillus sp. DP. 152 [J]. Journal of Fermentation and Bioengineering,1997,84(2):108-112.
    [60]曾常华,林波.新型生物絮凝剂的研究进展[J].环境科学与管理,2007,32(2):56.
    [61]马放,刘俊良,李淑更,等.复合菌生物絮凝剂的开发[J].中国给水排水,2003,19(4): 1-4.
    [62]张维杰.糖复合物生化研究技术[M].浙江:浙江大学出版社,1999:57-60.
    [63]肖琳,杨柳燕,尹大强,等.环境生物实验技术[M].北京:中国环境科学出版社,2004,7.
    [64]季树太.我国啤酒行业现状与发展前景展望[J].酿酒,2003,30(6):15-16.
    [65]邱建华.啤酒工业废水处理工艺方案浅析[J].闽西职业大学学报,2004,5(2):98-102.
    [66]陈亚平,付永胜,李湘梅,等.啤酒工业废水的特点及其处理方法[J].污染防治技术,2003,16(4):146-149.
    [67]杨英杰,王淑珍,杨家峰,等.以啤酒洗糟废水为主料产肮圆酵母液体发酵的研究[J].上海师范大学学报(自然科学版),2003,32(1):72-76.
    [68]Joung Han Yim, Sung Jin Kim, Se Hun Ahn, et al. Characterization of a novelbioflocculant, p-KG03, from a marine dinoflagellate[J]. Bioresource Technology,2007, 98(2):361-367.
    [69]Wu Ye, Characterzation and flocculating properties of an extracellular biopolymer produced from a Bacillus subtillis DYU1 isolate. Process Biochem.,2007,5,1-10.
    [70]Wang Z, Wang K, Xie Y. Bioflocculant-producing microorganisms. Acta Microbiol Sin., 1995,35:1-9.
    [71]战广琴,钱万英.生物化学实验[M].北京:中国农业大学出版社,2001:23-28.
    [72]邵雪玲,毛歆,郭一清.生物化学与分子生物实验指导[M].武汉:武汉大学出版社,2003,10:159-160.
    [73]Dubios M, Gilles KA, Rcbers PA, Smith F. Colorimetric method for determination of sugars and related substances[J]. Analytic Chemistry,1956,28(12):350-355.
    [74]奚旦立,孙裕生,刘秀英.环境监测[M].第三版.高等教育出版社,2004,7.103-105.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700