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外加水解酶强化剩余污泥水解和酸化的研究
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摘要
目前,高速城市化进程使污水处理厂产生的剩余污泥量大幅增加,其处理成为污水生物处理过程中面临的一个非常严峻的问题。污水处理厂用于剩余污泥处理和处置的费用大约占整个污水厂投资及运行费用的50%,甚至高达60%。污泥是一种富含有机质的物质,将其资源化利用,就能变废为宝。剩余污泥水解酸化的主要目的是改善污泥的生化降解性能,从而使较多的溶解性COD (SCOD)溶出和较多的短链脂肪酸(SCFAs)产生。SCOD和SCFAs,特别是SCFAs中的乙酸和丙酸,可以作为碳源物质强化生物除磷过程(EBPR)。因此,研究污水厂污泥水解和酸化过程具有重要的现实意义。为了达到此目的,本课题采用外加酶(中性蛋白酶和α-淀粉酶)来强化污泥水解产酸过程,从而为污泥处理过程提供一种新的方法。
     水解是污泥厌氧消化过程的限速步骤,而污泥中复杂有机质的水解主要取决于水解酶。然而,污泥中的水解酶含量较低,且这些酶一般隐藏、束缚、包埋在污泥基体内,活性没有得到表达,从而导致常规污泥处理过程的水解速率较低。目前,通过外加水解酶促进污泥水解的相关研究还比较少,本研究通过考察厌氧条件下单一酶和复合酶作用时,酶投加量、反应温度、酶配比等对城市污水处理厂剩余污泥破解及减量的影响,优化酶处理过程的指标。结果表明,在厌氧条件下,外加水解酶可以促进剩余污泥中颗粒态有机物的溶解、溶解态大分子有机物(蛋白质和碳水化合物)的水解以及水解后小分子有机物(氨基酸和单糖)的降解过程。该反应在4h内基本完成,淀粉酶比蛋白酶的水解效果好,复合酶的水解效果比单一酶的好。当水解温度为50℃,蛋白酶和淀粉酶的配比为1:3时,水解效果最佳,VSS去除率达68.24%。
     为了更清楚地了解外加水解酶强化污泥水解过程的本质特征,此过程的动力学分析与物质转化规律极为重要。以淀粉酶为例,对淀粉酶强化污泥水解过程动力学进行了探讨。结果表明,酶催化污泥水解反应在4h内基本完成,在此过程中,反应迅速,此后水解速率变缓。淀粉酶水解过程的阿仑尼乌斯方程为1nk=2429/T+5.57(R2=0.964)。此过程中的反应活化能可由空白组的62.72kJ/mol降低到20.19kJ/mol。污泥水解过程物质转化平衡分析表明:50℃时淀粉酶强化污泥水解过程底物与SCOD的转化系数α为0.266±0.012g SCOD/g VSS,与碳水化合物的转化系数α为0.043±0.001g碳水化合物/g VSS,与NH4+-N的转化系数为0.038±0.002g NH4+-N/g VSS。
     在酶强化污泥水解的基础上,就外加水解酶对污泥发酵产酸过程作进一步的研究,并从微观和宏观控制上探讨了酶强化污泥水解和酸化过程的机理及影响因素。结果表明,外加水解酶可以促进剩余污泥的发酵产酸过程。经不同水解酶处理后,乙酸始终是产量最大的有机酸,差不多占总有机酸产生量的50%,丙酸和异戊酸次之,正戊酸是产量最少的酸。在整个厌氧发酵过程中,不论是否投加酶,剩余污泥的pH值都随发酵时间的延长而升高;同时,投加水解酶的剩余污泥与空白试验组的pH值的变化趋势相同。
     探讨外加水解酶强化污泥水解的机理对于此过程内在和本质特征的了解具有重要的意义。目前,运用三维荧光光谱技术识别EPS和DOM的特性已有相关的研究,本研究即运用三维荧光光谱分析法来分析外加酶强化污泥厌氧消化过程中EPS和DOM的光谱特性及物质转化规律,以期从新的角度来探究酶强化剩余污泥水解过程的机理。通过三维荧光光谱分析表明,污泥中的荧光物质主要为蛋白质类物质(芳香蛋白和色氨酸)和腐殖酸类物质,其中色氨酸物质的溶出和转化速率高于芳香蛋白物质。水解酶会严重破坏EPS的结构和功能,同时复杂的DOM降解为低分子量的中间产物,继而促进污泥溶解和污泥降解。通过对比灭菌污泥与不灭菌污泥的有机酸产量和水解酶活力,证实了在外加酶存在的条件下,剩余污泥水解和发酵产酸是污泥中有机物被微生物降解的结果。通过利用PCR-DGGE结合DNA测序和系统发育分析对污泥水解酸化过程中微生物(主要是细菌)的群落结构进行多样性研究,表明原污泥和污泥水解发酵、产酸过程中存在的微生物有部分类似,但在各个阶段也具有各自特有的微生物菌群。投加水解酶的污泥水解产酸过程中梭酸菌群的含量较空白组中的多。
     外加水解酶和污泥中原有的水解酶会隐藏、束缚、包埋在污泥基体内,从而导致其利用效率较低。表面活性剂可以促进固相物质转化为液相物质,促使大量有机物质溶解于液相中,破坏了污泥絮体结构,将束缚和隐藏于污泥基体和细胞膜上的酶释放出来。同时,污泥中复杂有机物质的水解主要取决于水解酶。鉴于水解酶和表面活性剂两者的特性,表面活性剂和酶的联合作用会对污泥水解过程起到协同作用,其可以用来强化污泥的减量性能。最后,就酶和表面活性剂联合作用对污泥水解和酸化过程的影响进行了研究。结果表明,酶和表面活性剂的联合作用极大地促进了剩余污泥的水解和酸化效率,且两者共同处理的效果明显优于单独处理。SDS+ME厌氧产酸系统生成的有机酸中,乙酸是含量最高的酸,丙酸是含量第二的酸。
Rapid urbanization in many areas of the world has resulted in an increasing of waste activated sludge (WAS) from wastewater treatment plants (WWTPs), which has become a serious environmental issue. Costs for traditional treatment and disposal of WAS are quite expensive and would account for up to50%or60%of the total operating cost of WWTPs. Sludge is a kind of substance that are rich in organic matter, and it can be turn into wealth if rational use of the waste. The aim of hydrolysis and acidfication of WAS is to improve its biological degradability in the terms of higher soluble chemical oxygen demand (SCOD) and short chain fatty acids (SCFAs) productions. SCOD and SCFAs, especially acetate and propionate, are recognized as the most suitable carbon substrates for enhanced biological phosphorus removal (EBPR). Therefore, the hydrolysis and acidification of WAS has caused wide public concern, and it has important practical significance for sludge treatment. In order to reach the goal, the additional enzymes (protease and a-amylase) were selected to enhance the hydrolysis and acidification of WAS, thus provided a new technique for the treatment of WAS.
     Hydrolyis of particulate organic matter to soluble substance is believed to be the rate-limiting step of anaerobic digestion. The hydrolysis of complex organic molecules in the degradation of biodegradable particulate organic matter depends heavily on hydrolytic enzymes. However, the dosages of enzyme in the sludge are low, and they are usually entrapped by, adsorbed by, or bound to the sludge, thus leading to the low hydrolysis efficiency of the conventional sludge treatment. Recently, the enzymatic hydrolysis of sewage sludge has not been conclusively determined, thus the effect of enzyme dosage, operating temperature and the mixture ratio on the solubilisation of WAS were evaluated with additional enzymes used alone or in combination in this investigatin. It was found that during sludge anaerobic fermentation, the solubilization of sludge particulate organic-carbon and the hydrolysis of solubilized substrate (protein and carbohydrate) were all increased in the presence of enzyme. VSS solubilisation process could be almost completed within4h. Single enzyme had less impact on sludge solubilisation, of which amylase treatment displayed higher hydrolysis efficiency than that of protease. The mixture of two enzymes (protease:amylase=1:3) resulted in optimum hydrolysis result, the efficiency of solids hydrolysis could be increased to68.43%at the temperature of 50℃.
     In order to clearly understand the substantive characteristics of the hydrolysis process enhanced by enzyme, the kinetic analysis and the material transformation rule during this process is very important. The hydrolysis kinetics of WAS hydrolysis process enhanced by additional a-amylase was evaluated. The results showed that VSS solubilisation process could be almost completed within4h, and the rate constants obtained in this study followed the Arrhenius type of behavior. The Arrhenius equation of a-amylase hydrolysis (lnk=2429/T+5.57, R2=0.964), the reaction activation energy for VSS hydrolysis reduced from62.72kJ/mol (control test) to20.19kJ/mol (a-amylase treatment). Kinetics analysis indicated that the conversion coefficients (a) of VSS to soluble chemical oxygen demand (SCOD), carbohydrates and NH4+-N was found to be0.266±0.012,0.043±0.001and0.038±0.002, respectively.
     Based on the WAS hydrolysis enhanced by enzyme, the effect of enzyme on WAS acidification and the destruction mechanisms of WAS enhanced by additional enzymes was further analyzed and explored. It was found that enzyme could promote the hydrolysis and acidification of WAS. After different enzymes treated, acetic acid was the most prevalent product, which almost accounted for50%of the total SCFAs. The propionic and iso-valeric acids were the second, and the n-valeric acid was the lowest. During the entire fermentation, the pH values kept increasing no matter in the presence or absence of enzyme, and the same pH variations were observed.
     The study on the destruction mechanisms of WAS during anaerobic digestion is helpful for the understanding of substantive characteristics of the hydrolysis enhanced by enzyme. The Excitation-emission matrix (EEM) fluorescence spectroscopy has been applied in the distinguishing of the characteristics of extracellular polymeric substances (EPS) and dissolved organic matter (DOM), thus the objectives of this research were to obtain the EEM fluorescence characteristic of the EPS and DOM during WAS anaerobic digestion enhanced by enzymes and attempt to well understand this process from a novel insight. It was found that the protein-like (aromatic and tryptophan protein-like substances) and humic acid-like substances were the mainly fluorophores in the sludge, of which the release and transformation of tryptophan protein-like substances was more rapidly than that of aromatic protein-like substances. The EPS could be seriously disrupted by the action of hydrolytic enzymes, and the complex DOM was also broken down into low molecular-weight intermediates, thus the hydrolytic enzyme could enhance WAS solubilization and destruction. The comparisons of SCFAs production and hydrolytic enzymes activities between autoclaved and unautoclaved sludge showed that the production of SCFAs was the result of organics degraded by microbial. The diversity of microbial community structure (mainly bacterium) was studied through the application of16S rDNA-PCR amplification, DGGE fingerprinting and phylogenetic analysis. The results showed that the microbial existed in the enzymatic treatment and the raw sludge was partially similar, and each stage also had their special microbial. The amount of Clostridiaceae bacterium for the enzyme systems were much more than the blank during WAS hydrolysis and acidification
     The enzyme added or originally exist in the sludge are usually entrapped by, adsorbed by, or bound to the sludge, thus leading to the low hydrolysis efficiency of the conventional sludge treatment. Surfactant can cause an apparent increase in the aqueous solubility, thus accelerate the rate of nonaqueous phase substance dissolution into the aqueous phase, which may be able to compromise the floc integrity, liberate the trapped enzyme (within the floc matrix and on the cell-surface) and also expose more substrate. In addition, the hydrolysis of complex organic molecules in the degradation of biodegradable particulate organic matter depends heavily on hydrolytic enzymes. In consideration of the special characteristics of both enzyme and surfactant, the combination of surfactant and enzyme might exhibit a positive synergetic effect on waste solids hydrolysis, which could be used in the treatment of WAS to enhance its reduction. Thus, the combined effect of SDS and enzyme on WAS hydrolysis and acidification was investigated. It was found that the combined system was more effective in the promotion of sludge hydrolysis than sole SDS and sole enzyme. The composition analysis of SCFAs produced in SDS+mixed-enzymes (ME) system indicated that acetic acid was the most prevalent product and propionic acid was the second one.
引文
[1]Gray N F. Biology of wastewater treatment. UK:Oxford University Press,1989.
    [2]Spellman F R. Wastewater biosolids to compost. Lancaster, PA, USA:Technomic Publishing Company,1997.
    [3]Ginestet P. Comparative evaluation of sludge reduction routes. London:IWA Publishing,2007.
    [4]Gr(?)n C. Organic contaminants from sewage sludge applied to agricultural soils. Environ Sci. Pollut. Res. Int.,2007,14:53-60.
    [5]Campbell H W. Sludge management future issues and trends. Water Sci. Technol., 2000,41:1-8.
    [6]薛栋森.美国污水污泥的研究和利用概况.农业环境与发展,1991,1:31-33.
    [7]Abu-ghararah Z H, Randall C W. The effect of organic compounds on biological phosphorus removal. Water Sci. Technol.,1990,23:585-594.
    [8]Maurer M, Gujer W, Hany R, et al. Intracellular carbon flow in phosphorus accumulating organisms from activated sludge systems. Water Res.,1997,31: 907-917.
    [9]Lemos P C, Serafim L S, Reis M A. Synthesis of polyhydroxyalkanoates from different short-chain fatty acids by mixed cultures submitted to aerobic dynamic feeding. J. Biotechnol.,2006,122:226-238.
    [10]Pitman A R, Lotter L H, Alexander W V, et al. Fermentation of raw sludge and elutriation of resultant fatty acids to promote excess biological phosphorus removal. Water Sci. Technol.,1992,25:185-194.
    [11]Thomas M, Wright P, Blackall L, et al. Optimisation of Noosa BNR plant to improve performance and reduce operating costs. Water Sci. Technol.,2003,47: 141-148.
    [12]Chen Y G, Randall A A, McCue T. The efficiency of enhanced biological phosphorus removal from real wastewater affected by different ratios of acetic to propionic acid. Water Res.,2004,38:27-36.
    [13]Mahmood T, Elliott A. A review of secondary sludge reduction technologies for the pulp and paper industry. Water Res.,2006,40:2093-2112.
    [14]Wei Y, Van Houten R T, Borger A R, et al. Minimization of excess sludge production for biological wastewater treatment. Water Res.,2003,37: 4453-4467.
    [15]Low E W, Chase H A. Reducing production of excess biomass during wastewater treatment. Water Res.,1999,33:1119-1132.
    [16]卢年春,李萍,凌云,等.城市污泥综合利用研究.安徽农业科学,2005,33:2101-2103.
    [17]马溪平.厌氧微生物学与污水处理.北京:化学工业出版,2005,29-35.
    [18]任南琪,王爱杰.厌氧生物技术原理与应用.北京:化学工业出版社,2004,18-22.
    [19]Eastman J A, Ferguson J F. Solubilization of particulate organic carbon during the acid phase of anaerobic digestion. J. Water Pollut. Control Fed.,1981,53: 352-366.
    [20]Beijer R. Enzymatic treatment of wastewater sludge in presence of a cation binding agent-improved solubilisation and increased methane production:[dissertation]. Sweden:University of Linkopings,2008,49-50.
    [21]Ahuja S K, Ferreira G M, Moreira A R. Utilization of enzymes for environmental applications. Crit. Rev. Biotechnol.,2004,24:125-154.
    [22]Recktenwald M, Wawrzynczyk J, Dey E S, et al. Enhanced efficiency of industrial-scale anaerobic digestion by the addition of glycosidic enzymes. J. Environ. Sci. Heal. A Tox. Hazard. Subst Environ. Eng.,2008,43:1536-1540.
    [23]Goel R, Mino T, Satoh H, et al. Enzyme activities under anaerobic and aerobic conditions in activated sludge sequencing batch reactor. Water Res.,1998,32: 2081-2088.
    [24]Shanableh A, Jomaa S. Production and transformation of volatile fatty acids from sludge subjected to hydrothermal treatment. Water Sci. Technol.,2001,44: 129-135.
    [25]顾夏声,胡洪营,文湘华,等.水处理生物学-5版.北京:中国建筑工业出版社,2011,9-10.
    [26]Hu D, Lu H P. Placing single-molecule T4 lysozyme enzymes on a bacterial cell surface:Toward probing single-molecule enzymatic reaction in living cells. Biophys. J.,2004,87:656-661.
    [27]Moak M, Molineux I J. Peptidoglycan hydrolytic activities associated with bacteriophage virions. Mol. Microbiol.,2004,51:1169-1183.
    [28]Gill A O, Holley R A. Interactive inhibition of meat spoilage and pathogenic bacteria by lysozyme, nisin and ETA in the presence of nitrite and sodium chloride at 24℃. Int. J. Food Microbiol.,2003,80:251-259.
    [29]许强.污泥处理新技术.北京:化学工业出版社,2003,45-46.
    [30]Guo X S, Liu J X, Wei Y S, et al. Sludge reduction with Tubificidae and the impact on the performance of the wastewater treatment process. J. Environ. Sci., 2007,19:257-263.
    [31]Goel R, Mino T, Satoh H, et al. Comparison of hydrolytic enzyme systems in pure culture and activated sludge under different electron acceptor conditions. Water Sci. Technol.,1998,37:335-343.
    [32]Whiteley C G, Enongene G, Pletschke B I, et al. Co-digestion of primary sewage sludge and industrial wastewater under anaerobic sulphate reducing conditions: enzymatic profiles in a recycling sludge bed reactor. Water Sci. Technol.,2003, 48:129-138.
    [33]Whiteley C G, Burgess J E, Melamane X, et al. The enzymology of sludge solubilisation utilising sulphate-reducing systems:the properties of lipases. Water Res.,2003,37:289-296.
    [34]Gessesse A, Dueholm T, Petersen S B, et al. Lipase and protease extraction from activated sludge. Water Res.,2003,37:3652-3657.
    [35]Leal M C M R, Freire D M G, Cammarota M C, et al. Effect of enzymatic hydrolysis on anaerobic treatment of dairy wastewater. Process Biochem.,2006, 41:1173-1178.
    [36]Whiteley C G, Heron P, Pletschke B, et al.The enzymology of sludge solubilisation utilising sulfate reducing systems:Properties of proteases and phosphatases. Enzyme Microb. Tech.,2002,31:419-424.
    [37]Nybroe O, Jorgensen PE, Henze M, et al. Enzyme activities in waste water and activated sludge. Water Res.,1992,26:579-584.
    [38]Cadoret A, Conrad A, Block J C. Availability of low and high molecular weight substrates to extracellular enzymes in whole and dispersed activated sludges. Enzyme Microb. Tech.,2002,31:179-186.
    [39]Higuchi Y, Ohashi A, Imachi H, et al. Hydrolytic activity of alpha-amylase in anaerobic digested sludge. Water Sci. Technol.,2005,52:259-266.
    [40]Whiteley C, Pletschke B, Rose P, et al. Specific sulphur metabolites stimulate β-glucosidase activity in an anaerobic sulphidogenic bioreactor. Biotechnol. Lett., 2002,24:1509-1513.
    [41]Guellil A, Boualam M, Quiquampoix H, et al. Hydrolysis of wastewater colloidal organic matter by extracellular enzymes extracted from activated sludge flocs. Water Sci. Technol.,2001,43:33-40.
    [42]Yasunori Y. The method and device of the microbial sludge reduction. JPN kokai Tokkyo Koho,1994.
    [43]Masahiko M. The new micro-organisms. JPN kokai Tokkyo Koho,1997.
    [44]Yasumasa O. Biological treatment of sewage sludge. JPN kokai Tokkyo Koho, 2003.
    [45]Houghton J I, Quarmby J, Stephenson T. Municipal wastewater sludge dewaterability and the presence of microbial extracellular polymer. Water Sci. Technol.,2001,44:373-379.
    [46]Liu H, Fang H H. Extraction of extracellular polymeric substances (EPS) of sludges. J. Biotechnol.,2002,95:249-256.
    [47]Flemming H C, Wingender J. Relevance of microbial extracellular polymeric substances (EPSs)-part I:structural and ecological aspects. Water Sci. Technol. 2001,43:1-8.
    [48]Korstgens V, Flemming H C, Wingender J, et al. Influence of calcium ions on the mechanical properties of a model biofilm of mucoid Pseudomonas aeruginosa. Water Sci. Technol.,2001,43:49-57.
    [49]Park C, Novak J T. Characterization of activated sludge exocellular polymers using several cation-associated extraction methods. Water Res.,2007,41: 1679-1688.
    [50]Mikkelsen L H, Keiding K. Physico-chemical characteristics of full scale sewage sludges with implications to dewatering. Water Res.,2002,36:2451-2462.
    [51]Pei H Y, Hu W R, Liu Q H. Effect of protease and cellulase on the characteristic of activated sludge. J. Hazard. Mater.,2010,178:397-403.
    [52]Ayol A. Enzymatic treatment effects on dewaterability of anaerobically digested biosolids-I:performance evaluations. Process Biochem.,2005,40:2427-2434.
    [53]Ayol A, Dentel S K. Enzymatic treatment effects on dewaterability of anaerobically digested biosolids-II:laboratory characterizations of drainability and filterability. Process Biochem.,2005,40:2435-2442.
    [54]Parmar N, Singh A, Ward O P. Enzyme treatment to reduce solids and improve settling of sewage sludge. J. Ind. Microbiol. Biot.,2001,26:383-386.
    [55]Roman H J, Burgess J E, Pletschke B I. Enzyme treatment to decrease solids and improve digestion of primary sewage sludge. Afr. J. Biotechnol.,2006,5: 963-967.
    [56]Watson S D, Akhurst T, Whiteley C G, et al. Primary sludge floc degradation is accelerated under biosulphidogenic conditions:enzymological aspects. Enzyme Microb. Tech.,2004,34:595-602.
    [57]Dharmsthiti S, Kuhasuntisuk B. Lipase from Pseudomonas aeruginosa LP602: biochemical properties and application for wastewater treatment. J. Ind. Microbiol. Biot.,1998,21:75-80.
    [58]Felice B D, Pontecorvo G, Carfagna M. Degradation of waste waters from olive oil mills by Yarrowia lipolytica ATCC 20255 and Pseudomonas putida. Acta Biotechnol,,1997,17:231-239.
    [59]Palma M B, Pinto A L, Gombert A K, et al. Lipase production by Penicillium restrictum using solid waste of industrial babassu oil production as substrate. Appl. Biochem. Biotech.,2000,84:1137-1145.
    [60]Adav S S, Lee D J, Lai J Y. Proteolytic activity in stored aerobic granular sludge and structural integrity. Bioresource Technol.,2009,100:68-73.
    [61]Wawrzynczyk J, Dey E, Norrlow O, et al. Alternative method for sludge reduction using commercial enzymes. In:Eigth CIWEM/Aqua Enviro European Biosolids and Organic Residuals Conference. Wakefield, West Yorkshire, UK: 2003,1-5.
    [62]Warren R A J. Microbial hydrolysis of polysaccharides. Annu. Rev. Microbiol., 1996,50:183-212.
    [63]Naika G S, Tiku P K. Characterization of functional intermediates of endoglucanase from Aspergillus aculeatus during urea and guanidine hydrochloride unfolding. Carbohydr. Res.,2010,345:1627-1631.
    [64]Morais S, Heyman A, Barak Y, et al. Enhanced cellulose degradation by nano-complexed enzymes:Synergism between a scaffold-linked exoglucanase and a free endoglucanase. J. Biotechnol.,2010,147:205-211.
    [65]Domingues F C, Queiroz J A, Cabral J M, et al. The influence of culture conditions on mycelial structure and cellulase production by Trichoderma reesei Rut C-30. Enzyme Microb. Tech.,2000,26:394-401.
    [66]Xue Y P, Jin L Q, Liu Z Q, et al. Purification and characterization of beta-glucosidase from Reticulitermes flaviceps and its inhibition by valienamine and validamine. Afr. J. Biotechnol.,2008,7:4595-4601.
    [67]Hageskal G, Lima N, Skaar I. The study of fungi in drinking water. Mycol. Res., 2009,113:165-172.
    [68]Molla A H, Fakhrul-Razi A, Abd-Aziz S, et al. In-vitro compatibility evaluation of fungal mixed culture for bioconversion of domestic wastewater sludge. World J. Microb. Biot.,2001,17:849-856.
    [69]Fakhrul-Razi A, Alam M Z, Idris A, et al. Filamentous fungi in Indah Water Konsortium (IWK) sewage treatment plant for biological treatment of domestic wastewater sludge. J. Environ. Sci. Heal. A Tox. Hazard. Subst Environ. Eng., 2002,37:309-320.
    [70]Alam M Z, Fakhrul-Razi A, Molla A H. Biosolids accumulation and biodegradation of domestic wastewater treatment plant sludge by developed liquid state bioconversion process using a batch fermenter. Water Res.,2003,37: 3569-3578.
    [71]Alam M Z, Fakhrul-Razi A, Molla A H. Optimization of liquid state bioconversion process for microbial treatment of domestic wastewater sludge. J. Environ. Eng. Sci.,2003,2:299-306.
    [72]Fr(?)lund B, Griebe T, Nielsen P H. Enzymatic activity in the activated-sludge floc matrix. Appl. Microbiol. Biot.,1995,43:755-761.
    [73]Nielsen P H, Roslev P, Dueholm T E, et al. Microthrix parvicella, a specialized lipid consumer in anaerobic-aerobic activated sludge plants. Water Sci. Technol., 2002,46:73-80.
    [74]Van Ommen K F, Geesey G G. Localization and identification of populations of phosphatase-active bacterial cells sssociated with activated sludge flocs. Microb. Ecol.,1999,38:201-214.
    [75]Henze M, Grady C P L, Gujer W, et al. Activated Sludge Model No.1. IAWQ Scientific and Technical Reports No.1, London, UK,1986.
    [76]Henze M, Gujer W, Mino T, et al. Activated Sludge Model No.2. IAWQ Scientific and Technical Report No.3, London, UK,1995.
    [77]Henze M, Gujer W, Mino T, et al. Activated Sludge Models ASM1, ASM2, ASM2D and ASM3. IWA Scientific and Technical Report 9, IWA Publishing, Alliance House, London,2000.
    [78]Batstone D J, Keller J, Angelidaki I, et al. Anaerobic Digestion Model No.1. (ADM1). London:IWA Publishing,2002.
    [79]Yasui H, Goel R, Li Y Y, et al. Modified ADM1 structure for modelling municipal primary sludge hydrolysis. Water Res.,2008,42:249-259.
    [80]Vavilin V A, Rytov S V, Lokshina L Y. A description of hydrolysis kinetics in anaerobic degradation of particulate organic matter. Bioresource Technol.,1996, 56:229-237.
    [81]Boczar B A, Begley W M, Larson R J. Characterization of enzyme activity in activated sludge using rapid analyses for specific hydrolases. Water Environ. Res.,1992,64:792-797.
    [82]Watson S D, Pletschke B I. The effect of sulfide on a-glucosidases:implications for starch degradation in anaerobic bioreactors. Chemosphere,2006,65: 159-164.
    [83]Zhang X, Dennis P, Ehrenberg M, et al. Kinetic properties of rrn promoters in Escherichia coli. Biochimie,2002,84:981-996.
    [84]Lavallee B, Lessard P, Besser C. Decay rate variability of active heterotrophic biomass. Water Sci. Technol.,2002,46:423-430.
    [85]Lee D U, Casasus-Zambrana A, Hamilton R, et al. Significance of denitrifying enzyme dynamics in biological nitrogen removal processes:a simulation study. Water Sci. Technol.,2004,49:265-272.
    [86]Keiding K, Nielsen P H. Desorption of organic macromolecules from activated sludge:effect of ionic composition. Water Res.,1997,31:1665-1672.
    [87]Monique R, Elisabeth G N, Etienne P, et al. A high yield multi-method extraction protocol for protein quantification in activated sludge. Bioresource Technol., 2008,99:7464-7471.
    [88]Liao B Q, Allen D G, Droppo I G, et al. Surface properties of sludge and their role in bioflocculation and settleability. Water Res.,2001,35:339-350.
    [89]Wilen B M, Jin B, Lant P. The influence of key chemical constituents in activated sludge on surface and flocculating properties. Water Res.,2003,37:2127-2139.
    [90]Nielsen P H, Jahn A, Palmgren R. Conceptual model for production and composition of exopolymers in biofilms. Water Sci. Technol.,1997,36:11-19.
    [91]Yu G H, He P J, Shao L M, et al. Extracellula proteins, polysaccharides and enzymes impact on sludge aerobic digestion after ultrasonic pretreatment. Water Res.,2008,42:1925-1934.
    [92]Brown M J, Lester J N. Metal removal in activated sludge:the role of bacterial extracellular polymers. Water Res.,1979,13:817-837.
    [93]Chrost R J. Environmental control of the synthesis and activity of aquatic microbial ectoenzymes. In:Microbial enzymes in aquatic environments. New York:Springer-Verlag,1991,29-51.
    [94]Dey E, Szewczyk E, Wawrzynczyk J, et al. A novel approach for characterization of exopolymeric material in sewage sludge. J. Residuals Sci. Tech.,2006,3: 97-103.
    [95]Neis U. Intensification of biological and chemical processes by ultrasound. TU HH Reports on Sanitary Engineering,2002,35:79-90.
    [96]Zhang G M, Zhang P Y, Yang J M, et al. Ultrasonic reduction of excess sludge from the activated system. J. Hazard. Mater.,2007,145:515-519.
    [97]Bougrier C, Carrere H, Delgenes J P. Solubilisation of waste-activated sludge by ultrasonic treatment. Chem. Eng. J.2005,106:163-169.
    [98]Wang J, Wang J. Application of radiation technology to sewage sludge processing:a review. J. Hazard. Mater.,2007,143:2-7.
    [99]Chu L B, Wang J L, Wang B. Effect of gamma irradiation on activities and physicochemical characteristics of sewage sludge. Biochem. Eng. J.,2011,54: 34-39.
    [100]Prorot A, Julien L, Christophe D, et al. Sludge disintegration during heat treatment at low temperature:A better understanding of involved mechanisms with a multiparametric approach. Biochem. Eng. J.,2011,54:178-184.
    [101]Andreasan K, Peterson G, Thomsen H, et al. Reduction of nutrient emission by sludge hydrolysis. Water Sci. Technol.,1997,35:79-85.
    [102]Yan S, Miyanaga K, Xing X H, et al. Succession of bacterial community and enzymatic activities of activated sludge by heat-treatment for reduction of excess sludge. Biochem. Eng. J.,2008,39:598-603.
    [103]Wawrzynczyk J, Recktenwald M, Norrlow O, et al. The function of cation-binding agents in the enzymatic treatment of municipal sludge. Water Res.,2008,42:1555-1562.
    [104]Kim J R, Sim S J. Optimal conditions for improving enzyme pretreatment efficiency in sludge reduction process. Korean J. Microbiol. Biotechnol.,2004, 32:166-171.
    [105]Dursun D, Turkmen M, Abu-Orf M, et al. Enhanced sludge conditioning by enzyme pre-treatment:Comparison of laboratory and pilot scale dewatering results. Water Sci. Technol.,2006,54:33-41.
    [106]Sesay M L, Ozcengiz G, Dilek Sanin F. Enzymatic extraction of activated sludge extracellular polymers and implications on bioflocculation. Water Res.,2006,40: 1359-1366.
    [107]Gernaey K, Petersen B, Dochain D, et al. Modelling aerobic carbon source degradation processes using titrimetric data and combined respirometric-titrimetric data:structural and practical identifiability. Biotechnol. Bioeng.,2002,79754-767.
    [108]Elefsiniotis P, Oldham W K. Influence of pH on the acid-phase anaerobic digestion of primary sludge. J. Chem. Technol. Biot.,1994,60:89-96.
    [109]Hsu S T, Yang S T. Propionic acid fermentation of lactose by Propionibacterium acidipropionici:effects of pH. Biotechnol. Bioeng.,1991,38:571-578.
    [110]Zoetemeyer R J, Van den Heuvel J C, Cohen A. pH influence on acidogenic dissimilation of glucose in an anaerobic digestor. Water Res.,1982,16:303-311.
    [111]Yu H Q, Fang H H P. Acidogenesis of dairy wastewater at various pH levels. Water Sci. Technol.,2002,45:201-206.
    [112]Zheng X, Chen Y G, Liu C C. Waste activated sludge alkaline fermentation liquid as carbon source for biological nutrients removal in anaerobic followed by alternating aerobic-anoxic sequencing batch reactors. Biotechnol. Bioeng.,2010, 18:478-485.
    [113]Chanona J, Ribes J, Seco A, et al. Optimum design and operation of primary sludge fermentation schemes for volatile fatty acids production. Water Res., 2006,40:53-60.
    [114]吴志皓,唐尧基,李桂敏,等.荧光分析法在环境有机污染物分析中的应用.分析仪器,2005,4:13-19.
    [115]Haack M B, Lantz A E, Mortensen P P, et al. Chemometric analysis of in-line multi-wavelength fluorescence measurements obtained during cultivations with a lipase producing Aspergillus oryzae strain. Biotechnol. Bioeng.,2007,96: 904-913.
    [116]Morel E, Santamaria K, Perrier M, et al. Application of multi-wavelength fluorometry for on-line monitoring of an anaerobic digestion process. Water Res., 2004,38:3287-3296.
    [117]陆剑忠,吴海龙,孙翔宇,等.交替三线性分解算法结合区域变量选择同时分辨和定量测定二甲基苯酚异构体复杂体系.分析化学,2004,32:1278-1282.
    [118]刘佳,吴海龙,方冬梅,等.三维荧光二阶校正法用于血浆和尿液中柔红霉素的快速测定.分析化学,2008,36:316-320.
    [119]Baker A. Fluorescence excitation-emission matrix characterization of river waters impacted by a tissue mill effluent. Environ. Sci. Technol.,2002,36: 1377-1382.
    [120]Saadi I, Borisover M, Armon R, et al. Monitoring of effuent DOM biodegradation using fluorescence, UV and DOC messurements. Chemosphere, 2006,63:530-539.
    [121]黎司,吉芳英,周光明,等.三峡库区水体溶解有机质的荧光光谱特性.分析化学,2009,37:1328-1332.
    [122]王志刚,张文清,张玉钧,等.三维荧光光谱法分类测量水体浮游植物浓度. 中国环境科学,2008,28:136-141.
    [123]Chanyasak V, Kubota H. Carbon/organic nitrogen ratio in water extract as measure of composting degradation. J. Ferment. Technol.,1981,59:215-219.
    [124]Le Coupannec F, Morin D, Sire O, et al. Characterisation of dissolved organic matter (DOM) in landfill leachates using fluorescence excitation-emission matrix. Environ. Technol.,2000,21:515-524.
    [125]Baker A, Michael C. Fluorescence of leachates from three contrasting land fills. Water Res.,2004,38:2605-2613.
    [126]席北斗,魏自民,赵越,等.垃圾渗滤液水溶性有机物荧光谱特性研究.光谱学与光谱分析,2008,28:2605-2608.
    [127]Albrecht R, Joffre R, LePetit J, et al. Calibration of chemical and biological changes in cocomposting of biowastes using nearinfrared spectroscopy. Environ. Sci. Technol.,2009,43:804-811.
    [128]Yu G H, He P J, Shao L M. Novel insights into sludge dewaterability by fluorescence excitation-emission matrix combined with parallel factor analysis. Water Res.,2010,44:797-806.
    [129]Provenzano M R, de Oliveira S C, Silva M R, et al. Assessment of maturity degree of composts from domestic solid wastes by fluorescence and Fourier transform infrared spectroscopies. J. Agric. Food Chem.,2001,49:5874-5879.
    [130]Droussi Z, Dorazio V, Hafidi M, et al. Elemental and spectroscopic characterization of humic-acid-like compounds during composting,of olive mill by-products. J. Hazard. Mater.,2009,163:1289-1297.
    [131]Gone D L, Seidel J L, Batiot C, et al. Using fluorescence spectroscopy EEM to evaluate the efficiency of organic matter removal during coagulation-flocculation of a tropical surface water (Agbo reservoir). J. Hazard. Mater.,2009,172:693-699.
    [132]Chen W, Westerhoff P, Leenheer J A, et al. Fluorescence excitation-emission matrix regional integration to quantify spectra for dissolved organic matter. Environ. Sci. Technol.,2003,37:5701-5710.
    [133]Tang Z, Yu G H, Liu D Y, Xu D B, Shen Q R. Different analysis techniques for fluorescence excitation-emission matrix spectroscopy to assess compost maturity. Chemosphere,2011,82:1202-1208.
    [134]罗琨,杨麒,李小明,等.外加酶强化剩余污泥水解的研究.环境科学,2010,31:763-767.
    [135]Fr(?)lund B, Palmgren R, Keiding K, et al. Extraction of extracellular polymers from activated sludge using a cation exchange resin. Water Res.,1996,30:1749-1758.
    [136]Pinnekamp J. Effects of thermal pretreatment of sewage-sludge on anaerobic-digestion. Water Sci. Technol.,1989,21:97-108.
    [137]Knapp J S, Howell J A. Treatment of primary sewage sludge with enzymes. Biotechnol. Bioeng.,1978,20:1221-1234.
    [138]Ji R, Brune A. Digestion of peptidic residues in humic substances by an alkali-stable and humic-acid-tolerant proteolytic activity in the gut of soil-feeding termites. Soil Biol. Biochem.,2005,37:1648-1655.
    [139]Feng L Y, Yan Y Y, Chen Y G. Kinetic analysis of waste activated sludge hydrolysis and short-chain fatty acids production at pH 10. J. Environ. Sci-China, 2009,21:589-594.
    [140]Veeken A, Hamelers B. Effect of temperature on hydrolysis rate of selected biowaste components. Bioresource Technol.,1999,69:249-254.
    [141]Siegrist H, Vogt D, Garcia-Heras J L, et al. Mathematical model for meso-and thermophilic anaerobic sewage sludge digestion. Environ. Sci. Technol.,2002, 36:1113-1123.
    [142]Ferreiro N, Soto M. Anaerobic hydrolysis of primary sludge:influence of sludge concentration and temperature. Water Sci. Technol.,2003,47:239-246.
    [143]Zhang P, Chen Y G, Zhou Q. Effect of surfactant on hydrolysis products accumulation and short-chain fatty acids (SCFA) production during mesophilic and thermophilic fermentation of waste activated sludge:Kinetic studies. Bioresource Technol.,2010,101:6902-6909.
    [144]Tomei M C, Braguglia C M, Mininni G. Anaerobic degradation kinetics of particulate organic matter in untreated and sonicated sewage sludge:Role of the inoculums. Bioresource Technol.,2008,99:6119-6126.
    [145]Bolzonella D, Pavan P, Zanette M, et al. Two-Phase Anaerobic Digestion of Waste Activated Sludge:Effect of an Extreme Thermophilic Prefermentation. Ind. Eng. Chem. Res.,2007,46:6650-6655.
    [146]Ge H Q, Jensen P D, Batstone D J. Increased temperature in the thermophilic stage in temperature phased anaerobic digestion (TPAD) improves degradability of waste activated sludge. J. Hazard. Mater.,2011,187:355-361.
    [147]Ge H Q, Jensen P D, Batstone D J. Temperature phased anaerobic digestion increases apparent hydrolysis rate for waste activated sludge. Water Res.,2011, 45:1597-1606.
    [148]Cirne D G, Agbor V B, Bjornsson L. Enhanced solubilisation of the residual fraction of municipal solid waste. Water Sci. Technol.,2008,57:995-1000.
    [149]Flotats X, Palatsi J, Ahring B K, et al. Identifiability study of the proteins degradation model, based on ADM1, using simultaneous batch experiments. Water Sci. Technol.,2006,54:31-39.
    [150]Chen Y, Cheng J J, Creamer K S. Inhibition of anaerobic digestion process:a review. Bioresource Technol.,2008,99:4044-4064.
    [151]Liu T, Sung S. Ammonia inhibition on thermophilic aceticlastic methanogens. Water Sci. Technol.,2002,45:113-120.
    [152]Yu H Q, Zheng X J, Hu Z H, et al. High-rate anaerobic hydrolysis and acidogenesis of sewage sludge in a modified upflow reactor. Water Sci. Technol., 2003,48:69-75.
    [153]Zhang P, Chen Y G, Huang T Y, et al. Waste activated sludge hydrolysis and short-chain fatty acids accumulation in the presence of SDBS in semi-continuous flow reactors:Effect of solids retention time and temperature. Chem. Eng. J., 2009,148:348-353.
    [154]Wang Q, Kuninobu M, Ogawa H I, et al. Degradation of volatile fatty acids in highly efficient anaerobic digestion. Biomass Bioenerg.,1999,16:407-416.
    [155]Ahn Y H, Speece R E. Elutriated acid fermentation of municipal primary sludge. Water Res.,2006,40:2210-2220.
    [156]Suwannakham S, Yang S T. Enhanced propionic acid fementation by Propionibacterium acidipropionici mutant obtained by adaptation in a fibrous-bed bioreactor. Biotechnol. Bioeng.,2005,91:325-337.
    [157]Imai A, Fukushima T, Matsushige K, et al. Characterization of dissolved organic matter in effluents from wastewater treatment plants. Water Res.,2002,36: 859-870.
    [158]Wingender J, Neu T R, Flemming H C. Microbial Extracellular Polymeric Substances:Characterization, Structures and Function. Springer, Berlin, Heidelberg,1999.
    [159]Esparza-Soto M, Westerhoff P K. Fluorescence spectroscopy and molecular weight distribution of extracellular polymers from full-scale activated sludge biomass. Water Sci. Technol.,2001,43(6):87-95.
    [160]Marose S, Lindemann C, Scheper T. Two-dimensional fluorescence spectroscopy: a new tool for on-line bioprocess monitoring. Biotechnol. Prog.,1998,14: 63-74.
    [161]Chang I S, Lee C H. Membrane filtration characteristics in membrane-coupled activated sludge system-the effect of physiological states of activated sludge on membrane fouling. Desalination,1998,120:221-233.
    [162]Sheng G P, Yu H Q. Characterization of extracellular polymeric substances of aerobic and anaerobic sludge using three-dimensional excitation and emission matrix fluorescence spectroscopy. Water Res.,2006,40:1233-1239.
    [163]Chen W, Westerhoff P, Leenheer J A, et al. Fluorescence excitation-emission matrix regional integration to quantify spectra for dissolved organic matter. Environ. Sci. Technol.,2003,3.7:5701-5710.
    [164]Wang Z W, Wu Z C, Tang S J. Characterization of dissolved organic matter in a submerged membrane bioreactor by using three-dimensional excitation and emission matrix fluorescence spectroscopy. Water Res.,2009,43:1533-1540.
    [165]Coble P G. Characterization of marine and terrestrial DOM in seawater using excitation-emission matrix spectroscopy. Mar. Chem.,1996,51:325-346.
    [166]Ni B J, Fang F, Xie W M., et al. Characterization of extracellular polymeric substances produced by mixed microorganisms in activated sludge with gel-permeating chromatography, excitation-emission matrix fluorescence spectroscopy measurement and kinetic modeling. Water Res.,2009,43: 1350-1358.
    [167]Li W H, Sheng G P, Lu R, et al. Fluorescence spectral characteristics of the supernatants from an anaerobic hydrogen-producing bioreactor. Appl. Microbiol. Biot,2011,89:217-224.
    [168]Li W H, Sheng G P, Liu X W, et al. Characterizing the extracellular and intracellular fluorescent products of activated sludge in a sequencing batch reactor. Water Res.,2008,42:3173-3181.
    [169]Guo J S, Xu Y F. Review of enzymatic sludge hydrolysis. J. Bioremed. Biodegrad.,2011,2:130. doi:10.4172/2155-6199.1000130.
    [170]Yang Q, Luo K, Li X M, et al. Enhanced efficiency of biological excess sludge hydrolysis under anaerobic digestion by additional enzymes. Bioresource Technol.,2010,101:2924-2930.
    [171]Jiang S, Chen Y G, Zhou Q. Effect of sodium dodecyl sulfate on waste activated sludge hydrolysis and acidification. Chem. Eng. J.,2007,132:311-317.
    [172]Weemaes M P J, Verstraete W H. Evaluation of current wet sludge disintegration techniques. J. Chem. Technol. Biot.,1998,73:83-92.
    [173]Rani A, Porwal S, Sharma R, et al. Assessment of microbial diversity in effluent treatment plants by culture dependent and culture independent approaches. Bioresource Technol.,2008,99:7098-7107.
    [174]Wiegel J, Tanner R, Rainey F A. An introduction to the family Clostridiaceae. The Prokaryotes. New York:Springer,2006,654-678.
    [175]Kato S, Haruta S, Cui Z J, et al. Effective cellulose degradation by a mixed-culture system composed of a cellulolytic Clostridium and aerobic non-cellulolytic bacteria. FEMS Microbiol. Ecol.,2004,51:133-142.
    [176]Eriksson T, Borjesson J, Tjerneld F. Mechanism of surfactant effect in enzymatic hydrolysis of lignocellulose. Enzyme Microb. Technol.,2002,31: 353-364.
    [177]Fu J J, Jiang B, Cai W M. Effect of synthetic cationic surfactants on dewaterability and settleability of activated sludge. Int. J. Environ. Pollut.,2009, 37:113-131.
    [178]Herbert D, Philipps P J, Strange R E. Carbohydrate analysis. Methods Enzymolo.,1971,5B:265-277.
    [179]Lowry O H, Rosebrough N J, Farr A L, et al. Protein measurement with the Folin phenol reagent. J. Biol. Chem.,1951,193:265-275.
    [180]Feitkenhauer H. Anaerobic digestion of desizing wastewater:influence of pretreatment and anionic surfactant on degradation and intermediate accumulation. Enzyme Microb. Technol.,2003,33:250-258.
    [181]Helle S S, Duff S J, Cooper D G. Effect of surfactants on cellulose hydrolysis. Biotechnol. Bioeng.,1993,42:611-617.

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