Journal of Applied Microbiology 2001, 90, 337±342 Metabolic response of bio®lm to shear stress in ®xed-®lm culture Y. Liu and J.-H. Tay Environmental Engineering Research Center, School of Civil and Structural Engineering, Nanyang Technological University, Singapore 539/9/00: received 6 September 2000 and accepted 31 October 2000 Y . L I U A N D J . - H . T A Y . 2001. Aims: In a bio®lm reactor, detachment force resulting from hydraulic shear is a major factor that determines the formation and structure of steady state bio®lm. The metabolic response of bio®lm to change in shear stress was therefore investigated. Methods and Results: A conventional annular reactor made of PVC was used, in which shearing over the rotating disc surface was strictly de®ned. Results from the steady state aerobic bio®lm reactor showed that the bio®lm structure (density and thickness) and metabolic behaviour (growth yield and dehydrogenase activity) were closely related to the shear stress exerted on the bio®lm. Smooth, dense and stable bio®lm formed at relatively high shear stress. Higher dehydrogenase activity and lower growth yield were obtained when the shear stress was raised. Growth yield was inversely correlated with the catabolic activity of bio®lm. The reduced growth yield, together with the enhanced catabolic activity, suggests that a dissociation of catabolism from anabolism would occur at high shear stress. Conclusions: Bio®lms may respond to shear stress by regulating metabolic pathways associated with the substrate ¯ux ¯owing between catabolism and anabolism. A biological phenomenon, besides a simple physical effect, is underlying the observed relation between the shear stress and resulting bio®lm structure. Signi®cance and Impact of the Study: A hypothesis is proposed that the shear-induced energy spilling would be associated with a stimulated proton translocation across the cell membrane, which favours formation of a stronger bio®lm. This research may provide a basis for experimental data on bio®lm obtained at different shear stresses to be interpreted in relation to energy. INTRODUCTION Bio®lm is a promising biotechnology for wastewater treatment. Intensive research has shown that the morphological characteristics of bio®lm are important for the stability and performance of a bio®lm reactor. Detachment force is considered a dominant factor that strongly in¯uences the bio®lm structure and performance. In a bio®lm reactor, detachment force may result from hydraulic shear. Much research has been dedicated to the effects of the detachment force on the morphological characteristics and structures of Correspondence to: Dr Yu Liu, Environmental Engineering Research Center, School of Civil and Structural Engineering, Nanyang Technological University, 50 Nanyang Avenue, Singapore 639798 (e-mail: [email protected]). ã 2001 The Society for Applied Microbiology bio®lm (Rittmann 1982; Chang et al. 1991; Chen et al. 1998; Kwok et al. 1998). In the environmental engineering literature, it is generally considered that a higher detachment force makes the bio®lm denser and thinner. It has been hypothesized that a physical rather than a biological phenomenon is responsible for the observed relation between detachment force and the resulting bio®lm structure (Vieira et al. 1993; Chen et al. 1998). So far, little attention has been paid to the interrelationship of the metabolism of ®xed bacteria to detachment force. There is evidence that suspended cells can respond to hydraulic shear by altering their growth rate, morphology, cell size/density and metabolism (Nollert et al. 1991; Meijer et al. 1993; Moreira et al. 1995; Chen and Huang 2000). However, a clear correlation between the detachment force 338 Y. LIU AND J.-H. TAY and the resulting bio®lm metabolism is still lacking for ®xed®lm culture. The performance of a bio®lm reactor is directly associated with the metabolic activity of ®xed bacteria under given operational conditions. Similar to suspended culture, the metabolic network of ®xed bacteria basically includes interrelated catabolic and anabolic reactions. As one of the most important aspects, the relation between the detachment force and the energy metabolism of bio®lm has been little studied so far. Therefore, an attempt to show the effects of detachment force on energy metabolism and the structure of bio®lm is reported, and related mechanisms are discussed. M A T E R I A LS A N D M E T H O D S Experimental apparatus A conventional annular reactor made of PVC was used. It consists of two coaxial cylinders, a stationary outer cylinder and a rotating inner cylinder made up of a stack of recti®ed removable PVC discs. The liquid volume of the reactor is 4 l. This type of reactor has the advantage of providing constant shearing over the rotating disc surface. The diameter of the rotating disc is 23 cm. Polystyrene ®lms (20 ´ 3 cm) were attached to the side surfaces of the discs to serve as support material for bio®lm development. Operation of reactor Bacteria from a steady state, laboratory-scale, aerobicsettling-anaerobic reactor, fed with peptone as sole carbon source, were used as inoculum. The reactor was started under identical seeding conditions for each rotation speed of the discs. After the seeding period, the reactor was switched to once-through continuous ¯ow at a constant hydraulic retention time of 2 h. The synthetic substrate, containing peptone as sole carbon source, KH2PO4, Na2HPO4, NH4Cl, MgCl2, CaCl2 and FeCl3, was continuously fed into the reactor by a peristaltic pump. The in¯uent chemical oxygen demand (COD) concentration was kept at 200 mg l)1, equivalent to a volumetric loading rate of 2á4 kg COD m)3 day)1 for the experiments. The shear stress on bio®lm was controlled by the rotation speed of the disc in the range of 40±120 rev min)1 and was expressed as the tip velocity of the rotating disc in terms of meters per second. The temperature was kept constant at 25 ‹ 1°C, while dissolved oxygen (DO) was supplied by pre-aeration of the substrate solution. In order to maintain the DO concentration at above 4á0 mg l)1 in all experimental runs, a DO controller was employed to function as follows. Once the DO concentration of the reactor dropped below 4á0 mg l)1, the DO probe located at the middle of the reactor transmits a signal to the DO controller to activate the electro-valve controlling the oxygen supply. Analytical methods Bio®lm samples were collected at steady state, indicated by constant ef¯uent and ®xed biomass concentrations, from the removable ¯exible PS slides (8 ´ 3 cm). The slides were located on the middle disc of the reactor. The soluble COD concentration was analysed using the standard method (APHA 1995). The dry weight of ®xed biomass was also analysed by the standard method (APHA 1995). Bio®lm thickness was determined according to the method proposed by Trulear and Characklis (1982). The sample slide was placed on a microscope. The 10´ objective was lowered micrometre by micrometre until the bio®lm surface was in focus, and the micro-adjustment dial setting was recorded. The objective was then lowered further until the inert plastic surface was in focus. The difference between the two focus lengths was then compared with a calibration curve, and the bio®lm thickness was determined. The bio®lm thickness was then expressed as a mean value evaluated from at least 10 measurements along the slide for each sample. Ohashi and Harada (1994) also used this method to determine bio®lm thickness. The dehydrogenase activity of the bio®lm is measured by following the reduction of 2-(p-iodophenyl)-3-(p-nitrophenyl)-5-phenyl tetrazolium chloride (INT) to iodonitrotetrazolium (INT-formazan), according to the procedure established by Lopez et al. (1986) and then used by Lertpocasombut (1991). The INTformazan concentration is then determined spectrophotometrically at 490 nm. The speci®c INT-dehydrogenase activity of the bio®lm is expressed in terms of the optical density at 490 nm per milligram of dry weight of bio®lm. In fact, the speci®c INT-dehydrogenase activity closely correlates with electron transport system activity (Trevors 1984). According to Trulear and Characklis (1982), for steady state ®xed-®lm culture, the observed growth yield (Yobs) is calculated as the increase in biomass concentration, including both ®xed and detached biomass, divided by the corresponding decrease of COD concentration. RESULTS A series of experiments was conducted at different tip velocities (Vt) of the rotating disc, ranging between 0á48 and 1á45 m s)1. In the annular reactor, the tip velocity of the rotating disc acts as a major shear stress on bio®lm (Rittmann 1982; Trulear and Characklis 1982). The tip velocity vs steady state bio®lm thickness and density is presented in Fig. 1. Results indicate that a higher tip velocity leads to a thinner and denser bio®lm, i.e., a compact bio®lm structure. Figure 2 shows the effects of Vt on the observed growth yield (Yobs) and speci®c INT-dehydrogenase activity of the bio®lm. The reduced Yobs and increased INT-dehydrogenase activity are observed with the increase ã 2001 The Society for Applied Microbiology, Journal of Applied Microbiology, 90, 337±342 RESPONSE OF BIOFILM TO SHEAR STRESS Fig. 1 Effect of tip velocity on the thickness and density of bio®lm. (·) Thickness; (s) density Fig. 2 Effect of tip velocity on Yobs and speci®c INT-dehydrogenase activity of bio®lm. (m)Yobs; (n) speci®c INT-dehydrogenase activity in tip velocity. In a three-phase ¯uidized bed reactor, Lertpocasombut (1991) also found that the INT-dehydrogenase activity of bio®lm was increased from 3á2 to 7á8 Absorbance (Abs) mg)1 dry weight as the speci®c velocity of air was shifted from 5á7 m h)1 to 10á2 m h)1. The interrelationship of the growth yield to INT-dehydrogenase activity is further shown in Fig. 3. The growth yield is apparently inversely dependent on the INT-dehydrogenase activity of the bio®lm. During the aerobic oxidation process, the respiratory activity of cells can be indirectly determined by measurement of the proton translocation activity, and the INT can be used as arti®cial proton acceptor to quantify the catabolic activity of the bio®lm. In order to demonstrate the possible interrelationship of catabolic activity of the bio®lm to the resulting bio®lm structure, bio®lm density vs speci®c INTdehydrogenase activity of the bio®lm is shown in Fig. 4. A clear correlation between the catabolic activity of the bio®lm 339 Fig. 3 Relationship between Yobs and speci®c INT-dehydrogenase activity of bio®lm Fig. 4 Relationship between bio®lm density and speci®c INT-dehydrogenase activity of bio®lm and the bio®lm density can be seen. These results suggest that a higher catabolic activity of bio®lm would favour formation of a stronger bio®lm. It appears from Figs 1, 2, 3 and 4 that the shear stress not only in¯uences the bio®lm structures, but also has a signi®cant effect on the energy metabolism of the bio®lm. DISCUSSION Effect of shear stress on bio®lm structure Figure 1 shows that a higher shear stress results in a thinner and denser bio®lm. Similar phenomena have also been reported in the literature (Chang et al. 1991; Vieira et al. 1993; Ohashi and Harada 1994; Chen et al. 1998). In addition, bio®lm density was found to correlate very closely with the self-immobilization strength of ®xed bacteria, which was dependent on the shear stress exerted on the ã 2001 The Society for Applied Microbiology, Journal of Applied Microbiology, 90, 337±342 340 Y. LIU AND J.-H. TAY bio®lm (Ohashi and Harada 1994; Chen et al. 1998). This, and previous research, suggests that hydrodynamic conditions have a signi®cant in¯uence on the density of bio®lm. It has been hypothesized in the literature that a physical phenomenon is responsible for the observed relation between detachment force and bio®lm structure (Vieira et al. 1993). However, the results in Figs 2 and 4 exhibit an interrelationship between bio®lm metabolism and shear stress. Response of bio®lm to shear stress To date, the mechanism by which ®xed bacteria respond to a shear stress and further produce a compact bio®lm has been unclear in a metabolic sense. In Fig. 2, a remarkable reduction in Yobs is observed when the shear stress, in terms of tip velocity of the rotating disc, increases, while the high shear stress on the bio®lm leads to a signi®cant increase in speci®c INT-dehydrogenase activity. It has been shown that the speci®c INT-dehydrogenase activity is very highly correlated with the electron transport system that determines catabolic activity of micro-organisms (Trevors 1984; Lopez et al. 1986). The higher catabolic activity implies that the more organic carbon should go to carbon dioxide. In fact, it has been demonstrated that growth yield is a function of the ratio between carbon channeled into carbon dioxide by catabolism and that converted to biomass through anabolism in suspended culture (Liu 1999). Therefore, the observed variations in growth yield and speci®c INTdehydrogenase activity in Fig. 2 may represent stimulated catabolic activity compared with anabolism. This, in turn, implies that a discrepancy between the rate of energy production by catabolism and the rate of energy utilization by anabolism would occur at high shear stress. A similar Yobs variation pattern with detachment force has also been observed in a steady state bio®lm airlift suspension reactor (Kwok et al. 1998). These observations suggest that bio®lms may indeed respond to shear stress by regulating metabolic pathways associated with the substrate ¯ux ¯owing between catabolism and anabolism. Fig. 5 Effect of speci®c velocity of air on Yobs and rO2/rTOC in a steady state, three-phase, ¯uidized bed reactor (Lertpocasombut 1991). (m) Yobs; (n) rO2/rTOC In this case, the speci®c velocity of air can re¯ect shear stress in the reactor. Similar to Fig. 2, Fig. 5 shows that higher shear stress results in a lower growth yield and a stimulated DO consumption rate. In fact, the biochemical reactions associated with bacterial metabolism result in an approximately linear relationship between oxygen utilization and carbon dioxide production (Selna and Schroeder 1979). In a metabolic sense, the rO2/rTOC ratio thus represents carbon distribution in the metabolic network of bacteria. The reduced growth ef®ciency, together with the increased rO2/ rTOC ratio, seems to suggest energy uncoupling between catabolism and anabolism. A direct relationship between Yobs and the rO2/rTOC ratio is further given in Fig. 6. Similar to Fig. 3, it is observed again that Yobs is inversely dependent on the catabolic activity of the bio®lm. As noted above, oxygen utilization and cell production oppose one another, and the more oxygen used in carbon dioxide production, the fewer cells are produced. Results reported by Trinet et al. (1991) and Rittmann et al. (1992) also showed that the ratio of carbon dioxide-carbon to bio®lm- Literature data Lertpocasombut (1991) studied the kinetics of bio®lm developed in a three-phase ¯uidized bed reactor coupled to a quadrupole mass spectrometer, and determined the growth yield, dissolved oxygen (DO) utilization rate (rO2) and total organic carbon (TOC) removal rate (rTOC). The effects of the speci®c velocity of air on the observed growth yield and rO2/rTOC ratio are shown in Fig. 5 for steady state bio®lm. In the study of Lertpocasombut (1991), only the speci®c velocity of air varied in the experiments, while the carrier concentration and water velocity were kept constant. Fig. 6 Relationship between Yobs and rO2/rTOC (Lertpocasombut 1991) ã 2001 The Society for Applied Microbiology, Journal of Applied Microbiology, 90, 337±342 RESPONSE OF BIOFILM TO SHEAR STRESS carbon increased with increasing shear stress in a steady state ¯uidized bed reactor. On the other hand, Vanderborght and Gilliard (1981) observed that up to 89% of the organic carbon was oxidized to carbon dioxide in the same type of reactor. This evidence from the literature supports a shear stress-induced metabolic shift in bio®lm culture. Shear stress-induced proton translocation: an hypothesis In the aerobic oxidation process, ATP is generated by oxidative phosphorylation in which process electrons are transported through the electron transport system from an electron donor (substrate) to a ®nal electron acceptor (oxygen) (Mitchell 1961; Wolfe 1993). On the other hand, the respiratory activity of aerobic bacteria couples with proton translocation activity, and a clear linkage of oxygen reduction to proton translocation has been shown (Babcock and Wikstrom 1992). Thus, it appears that the respiratory activity of aerobic bacteria can be indirectly determined by the measurement of proton translocation activity, and the INT can be used as arti®cial proton acceptor to quantify the catabolic activity of bio®lm. In this case, the magnitude of the speci®c INT-dehydrogenase and oxygen uptake activities can be used to describe the activity of proton translocation across the cell membrane, i.e., the INTdehydrogenase and oxygen utilization activities would be linked to the activity of proton diffusion across the cell membrane. As discussed earlier, shear stress-induced energy uncoupling can be seen as the increase in speci®c INTdehydrogenase activity and oxygen uptake rate, as shown in Figs 2 and 5. In fact, under the energy uncoupling state of cells, stimulated respiration activity was also observed in suspended microbe cultures (Mayhew and Stephenson 1998). Russell and Cook (1995) reported that futile cycles of protons would operate whenever there was an imbalance of catabolic and anabolic rates, and would be responsible for most of the observed energy spilling which led to lower growth ef®ciency. Further, a linear correlation between the rate of energy spilling and ¯ux of protons across the cell membrane was shown (Cook and Russell 1994). Therefore, it appears that the shear stress-induced INT-dehydrogenase and oxygen uptake activities could re¯ect facilitated proton diffusion across the cell membrane. It has been reported that acidi®cation is a common response to the cells subjected to high shear stress in suspended cell cultures (Meijer et al. 1993; Chen and Huang 2000). In fact, Chen and Huang (2000) found that high shear stress could induce proton elicitation in a suspended Stizolobium hassjoo culture. 341 Effect of shear-induced proton translocation on bio®lm structure It has been reported that proton translocation would have the following consequences in relation to surface characteristics of cells. (i) High proton ¯ux across the cell membrane leading to enhanced hydrophobic interaction of cells (Tay et al. 2000). (ii) Proton conductance across the cell membrane could induce surface dehydration (Babcock and Wikstrom 1992; Deamer and Akeson 1994; Tay et al. 2000). (iii) The proton translocating activity could induce the protonation and membrane fusion of the cell surface (Liu 1989; Babcock and Wikstrom 1992). (iv) The biovolume of cells would be condensed by up to 50% when catabolic activity was stimulated (Zubay 1984; Shen and Wang 1991). In general, the surface of micro-organisms is negatively charged under normal pH conditions. Obviously, increased proton translocation activity would decrease the net negative charge of the cell surface, and further promote cell±cell interaction. As noted above, one of the most important consequences of enhanced proton translocation is an increase in hydrophobic characteristics of the cell surface. In fact, there is strong evidence that the hydrophobicity of the cell surface is an important af®nity force in the selfimmobilization and attachment of cells (Marshall and Gruickshank 1973; Pringle and Fletcher 1983; van Loosdrecht et al. 1987). It had been reported that bio®lm density is proportionally related to the self-immobilization strength of ®xed bacteria, which, in turn, is determined by the shear stress on the bio®lm surface (Ohashi and Harada 1994; Chen et al. 1998). Recent research on microbe granulation has shown that the proton translocation-induced dehydration of the cell surface could facilitate and strengthen the cell±cell interaction and further, result in a high density of the microbial community (Tay et al. 2000; Teo et al. 2000). The proton translocation-strengthened structure of the microbe community had also been observed in suspended cultures. Low et al. (2000) reported that in media supplemented with an organic protonophore, para-nitrophenol (pNP), cell agglomerates formed dense ¯ocs compared with pNP-free cultures. This suggests that shear stress-induced proton translocation could facilitate and strengthen the cell±cell interaction and further, result in the high density of adhering cells, as observed in Fig. 4. It appears from the above discussion that when shear stress on the bio®lm is high, the bio®lm community would have to regulate its metabolic pathway so as to maintain a balance with the external detachment force through consuming non-growth-associated energy. As Russell and Cook (1995) noted, energy spilling is probably not a fortuitous act, and may be a mechanism for protecting bacteria from stressful environmental conditions and potentially toxic schemes of substrate metabolism. ã 2001 The Society for Applied Microbiology, Journal of Applied Microbiology, 90, 337±342 342 Y. LIU AND J.-H. TAY REFERENCES APHA (1995) Standard Methods for the Examination of Water and Wastewater 19th edn. Washington, D.C.: American Public Health Association. Babcock, G.T. and Wikstrom, M. (1992) Oxygen activation and the conservation of energy in cell respiration. Nature 356, 301±309. Chang, H.T., Rittmann, B.E., Amar, D., Heim, R., Ehrlinger, O. and Lesty, Y. (1991) Bio®lm detachment mechanisms in a liquid ¯uidized bed. Biotechnology and Bioengineering 38, 499±506. Chen, M.J., Zhang, Z. and Bott, T.R. (1998) Direct measurement of the adhesive strength of bio®lms in pipes by micromanipulation. Biotechnology Techniques 12, 875±880. Chen, S.Y. and Huang, S.Y. (2000) Shear stress effects on cell growth and L-DOPA production by suspension culture of Stizolobium hassjoo cells in an agitated bioreactor. Bioprocess Engineering 22, 5±12. Cook, G.M. and Russell, J.B. (1994) Energy-spilling reactions of Streptococcus bovis and resistance of its membrane to proton conductance. Applied and Environmental Microbiology 60, 1942±1948. Deamer, D.W. and Akeson, M. (1994) Role of water in proton conductance across model and biological membranes. In Biomembrane Electrochemistry ed. Blank, M. and Vodynoy, I. pp. 3±25. Washington: ACS. Kwok, W.K., Picioreanu, C., Ong, S.L., van Loosdrecht, M.C.M., Ng, W.J. and Heijnen, J.J. (1998) In¯uence of biomass production and detachment force on bio®lm structures in a bio®lm airlift suspension reactor. Biotechnology and Bioengineering 58, 400±407. Lertpocasombut, K. (1991) Epuration carboneÂe par ®lm biologique mince dans un reÂacteur aÁ lit ¯uidise triphasique. PhD Thesis, Institut National des Sciences AppliqueÂes-Toulouse, France. Liu, S.S. (1989) A new function of proton pumps in membrane fusion. In Current Biochemical Research in China ed. Zhou, C.L. pp. 161±171. New York: Academic Press. Liu, Y. (1999) Model of dissolved organic carbon distribution for substrate-suf®cient continuous culture. Biotechnology and Bioengineering 65, 474±479. Lopez, J.M., Koopman, B. and Bitton, G. (1986) INT-dehydrogenase test for activated sludge process control. Biotechnology and Bioengineering 28, 1080±1085. Low, E.W., Chase, H.A., Milner, M.G. and Curtis, T.P. (2000) Uncoupling of metabolism to reduce biomass production in the activated sludge process. Water Research 34, 3204±3212. Marshall, K.C. and Gruickshank, R.H. (1973) Cell surface hydrophobicity and the orientation of certain bacteria at interfaces. Archive of Microbiology 91, 29±40. Mayhew, M. and Stephenson, T. (1998) Biomass yield reduction: is biochemical manipulation possible without affecting activated sludge process ef®ciency. Water Science and Technology 38, 137±144. Meijer, J.J., Hoopen, T., Luyben, H.J.G. and Libbenga, A.M. (1993) Effects of hydrodynamic stress on cultured plant cells: a literature survey. Enzyme Microbial Technology 15, 234±238. Mitchell, P. (1961) Coupling of phosphorylation to electron and hydrogen transfer by a chemiosmotic type of mechanism. Nature 191, 144±148. Moreira, J.L., Alves, P.M., Aunins, J.G. and Carrondo, M.J.T. (1995) Hydrodynamic effects on BHK cells grown as suspended natural aggregates. Biotechnology and Bioengineering 46, 351±360. Nollert, M.U., Diamond, S.L. and Mclntire, L.V. (1991) Hydrodynamic shear stress and mass transport modulation of endothelial cell metabolism. Biotechnology and Bioengineering 38, 588±602. Ohashi, A. and Harada, H. (1994) Adhesion strength of bio®lm developed in an attached-growth reactor. Water Science and Technology 29, 281±288. Pringle, J.H. and Fletcher, M. (1983) In¯uence of substratum wettability on attachment of fresh bacteria to solid surface. Applied and Environmental Microbiology 45, 811±817. Rittmann, B.E. (1982) The effect of shear stress on bio®lm loss rate. Biotechnology and Bioengineering 24, 501±506. Rittmann, B.E., Trinet, F., Amar, D. and Chang, H.T. (1992) Measurement of the activity of a bio®lm: effects of surface loading and detachment on a three-phase liquid ¯uidized bed reactor. Water Science and Technology 26, 585±594. Russell, J.B. and Cook, G. (1995) Energetics of bacterial growth: balance of anabolic and catabolic reactions. Microbiology Review 59, 48±62. Selna, M.W. and Schroeder, E.D. (1979) Response of activated sludge processes to organic transient II-stoichiometry. Journal of Water Pollution Control Federation 51, 150±157. Shen, T. and Wang, J.Y. (1991) Biochemistry. Beijing: High Education Press. Tay, J.H., Xu, H.L. and Teo, K.C. (2000) Molecular mechanism of granulation. I: H+ translocation-dehydration theory. Journal of Environmental Engineering 126, 403±410. Teo, K.C., Xu, H.L. and Tay, J.H. (2000) Molecular mechanism of granulation. II: Proton translocating activity. Journal of Environmental Engineering 126, 411±418. Trevors, J.T. (1984) The measurement of electron transport system (ETS) activity in freshwater sediment. Water Research 18, 581±584. Trinet, F., Heim, R., Amar, D., Chang, H.T. and Rittmann, B.E. (1991) Study of bio®lm and ¯uidization of bioparticles in a threephase ¯uidized-bed reactor. Water Science and Technology 23, 1347±1354. Trulear, M.G. and Characklis, W.G. (1982) Dynamics of bio®lm processes. Journal of Water Pollution Control Federation 9, 1288±1301. Vanderborght, J.P. and Gilliard, C. (1981) BOD removal in ¯uidized beds: high biomass concentration or high oxygen transfer. In Biological Fluidized Bed Treatment of Water and Wastewater ed. Cooper, P.F. and Atkinson, B. pp. 383±389. Chichester: Ellis Horwood. van Loosdrecht, M.C.M., Lyklema, J., Norde, W., Schraa, G. and Zehnder, A.J.B. (1987) The role of bacterial cell wall hydrophobicity in adhesion. Applied and Environmental Microbiology 53, 1893±1897. Vieira, M.J., Melo, L.F. and Phinheiro, M.M. (1993) Bio®lm formation: Hydrodynamic effects on internal diffusion and structure. Biofouling 7, 67±80. Wolfe, S.L. (1993) Molecular and Cellular Biology. Wadsworth Publications Co. Belmont, California, USA. Zubay, G. (1984) Biochemistry. Addison-Wesley Publishing Company, New York, USA. ã 2001 The Society for Applied Microbiology, Journal of Applied Microbiology, 90, 337±342
© Copyright 2026 Paperzz