Attachment and adhesion force between biogas bubbles and anaerobic granular sludge in the up-flow anaerobic sludge blanket
Graphical abstract
Introduction
Over the past decades, anaerobic digestion has been widely used in the management of wastes and wastewaters as it reduces organic pollutants and produces renewable energy (Nguyen and Khanal, 2018). Moreover, it has undergone significant improvement due to the use of bio-reactors that are based on granular sludge (Zhang et al., 2012). Among them, up-flow anaerobic sludge blanket (UASB) is one of the most widely used high-rate anaerobic reactors for sewage treatment (Lettinga, 2001). The performance of a UASB is significantly influenced by the mixing of wastewater with anaerobic granular sludge (AGS), which is governed by the hydrodynamics of the reactor (Kundu et al., 2014). The characteristics of hydrodynamics in a UASB have been studied extensively under different conditions (Batstone et al., 2005; Peña et al., 2006; Ren et al., 2009). In previous papers, granular settlement in UASB was considered as Stokes flow, having a Reynolds number lower than 1 (Gupta and Gupta, 2005; Laguna et al., 1999). However, further research indicated that the Reynolds number of AGS in the typical UASB reactor fell in an intermediate flow regime category, with the Reynolds number between 1 and 500 (Tassew et al., 2019). Computational fluid dynamics (CFD) with Eulerian-Eulerian model has often been used to characterize and optimize the hydrodynamics in a UASB (Wei et al., 2019). However, the gas phase in this model is considered as a continuum, similar to the liquid phase. Though the influence of hydrodynamic conditions on mass transfer, AGS size distribution, and biogas production are well studied (Afridi et al., 2017; Wu et al., 2012a, 2012b), little is known about the interaction between biogas bubbles and AGS.
AGS has pores, channels, and cavities, which are conducive to the transport of nutrients, metabolites, and biogas bubbles (Jiang et al., 2016). Jiang et al. (2016) proposed that the micro-bubbles of biogas inside AGS diffused toward large-size channels to form an observable bubble on AGS. At a certain time, the bubble detaches from the surface of AGS to form a crater. In addition, extracellular polymeric substances (EPS) that are located outside AGS govern the mass transfer of substances and products (Sheng et al., 2010). As biogas bubbles must pass through the EPS layer before detaching from AGS into the liquid phase, EPS might play a crucial role in the interaction between biogas bubbles and AGS. Hence, the interaction between gas phase and solid phase, especially the single bubble and AGS, has not been described suitably.
The impinging-jet technique (Fig. 1A) was initially used in the deposition of latex particles on glass surfaces (Dabroś and van de Ven, 1983; Dabros and Vandeven, 1987). Then it was successfully used to describe the particle and submicron colloidal particles deposition (Dijt et al., 1990; Sanders et al., 1995). Furthermore, Yang et al. (2003) measured the attachment of bubble flux onto a solid surface in an impinging-jet stagnation flow, indicating that both electrolyte concentration and hydrodynamic flow were key factors for the attachment flux. Hence, the impinging-jet technique might provide direct information on the attachment between biogas bubbles and AGS.
Even though both impinging-jet technique and CFD can describe the hydrodynamics of UASB, there is a difficulty to directly observe the interaction forces between biogas bubbles and AGS at a single-particle level. Atomic force microscope (AFM), a powerful tool for sensitive force measurements, has been widely used to quantitatively measure the interaction forces between a bubble and the surface of solids or cells (Cui et al., 2016; Ditscherlein et al., 2018; Xie et al., 2015). It has led to further understanding of many physical and biological processes, such as mining, froth flotation, and fermentation (Liu et al., 2019; Wang et al., 2009; Zhang et al., 2017). The bubble probe AFM technique, where a gas bubble anchored on a tipless cantilever, was applied as a force probe to measure the interaction forces between a bubble and substrates (Tabor et al., 2011a, 2011b; Vakarelski et al., 2008; Xie et al., 2015). With the help of this technique, previous studies investigated the interaction of a bubble and particles under different conditions (Cui et al., 2017; Xie et al., 2015). Furthermore, Nguyen et al. (2003, 2004) indicated that the repulsive force between a bubble and a hydrophilic particle increased with increasing approach velocities of AFM tips. This bubble probe AFM technique with different approach velocities might provide a new insight into the interaction between a biogas bubble and AGS, which has important benefits on the optimization of hydrodynamics in UASB.
For the first time, the interaction between AGS and biogas bubble is investigated in this study both by impinging-jet technique and bubble probe AFM technique. The attachment between biogas bubbles (CO2 and CH4) and AGS at different Reynolds numbers was studied using impinging-jet technique. In addition, the adhesion force between a biogas bubble (CO2 and CH4) and AGS was also studied by bubble probe AFM at different approach velocities. These results may contribute to a better and new insight into the understanding of surface interaction between biogas bubbles and AGS in UASB.
Section snippets
Impinging-jet experiment
The impinging-jet experiment system is shown in Fig. 1A. Two kinds of AGS were collected from UASB treating wastewaters of beer factory (AGSb) and protein factory (AGSp), respectively. The characteristics of these two kinds of AGS are shown in Table 1. The solution in the impinging-jet apparatus was 0.9% NaCl (m/v). The AGS was washed three times with 0.9% NaCl and fixed on to the glass plate (diameter of 6.50 cm) with epoxy glue in one layer. The gas bubbles were generated using a capillary
Bubble-attachment on AGS
The attachment of bubbles and AGS is considered to occur when the bubbles attach to the AGS layer, excluding the bubbles attached to the AGS layer for a short duration (less than 1 s) and then are swept away by the flow. A typical video of bubble-attachment is shown in the Supporting Information. Based on the feature of impinging-jet technique, the bubble-attachment flux is uniform near the stagnation point. Fig. S3 shows the time-dependent change of normalized bubble-attachment density of CH4
Discussions
Bubble transport in UASB is mainly driven by hydrodynamic forces. The first step in successfully attaching the bubbles onto solids, such as AGS, was enough contact time for both bubbles and the AGS surface, so that the bubbles could deform and slide along the AGS surface to reach the maximum collision angle. Then, the liquid film between the bubble and AGS surface was thinned to a critical thickness and ruptured to form a three-phase contact. This three-phase contact was expansion and formation
Conclusions
To our best knowledge, this is the first study that applies impinging-jet technique and bubble probe AFM to explore the interaction between bubbles and anaerobic granular sludge (AGS) in UASB. The results obtained revealed that the fluxes of normalized CH4 or CO2 bubble-attachment onto AGS decreased with an increase in the Reynolds number due to the change in collision angle and the enhancement of the liquid film. In addition, for the more hydrophobic surface and oxygen-containing functional
Declaration of competing interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgements
This work was supported by the National Natural Science Foundation of China (No. 21776163, No. 51478453), Shandong Provincial Natural Science Foundation (ZR2019JQ18), the Qilu Youth Talent Programme of Shandong University, the Major Science and Technology Program for Water Resources of Shandong Province (SDSLKY201805), the Young creative research groups for interdisciplinary science in Shandong University (2020QNQT014).
References (63)
- et al.
Insight into mass transfer by convective diffusion in anaerobic granules to enhance biogas production
Biochem. Eng. J.
(2017) - et al.
Influence of bubble approach velocity on liquid film drainage between a bubble and a spherical particle
Powder Technol.
(2018) - et al.
In-situ biogas upgrading in thermophilic granular UASB reactor: key factors affecting the hydrogen mass transfer rate
Bioresour. Technol.
(2016) - et al.
Enhancing flotation performance of low rank coal by improving its hydrophobicity and the property of oily bubbles using 2-ethylhexanol
Int. J. Miner. Process.
(2017) - et al.
On the stability of bubbles trapped at a solid–liquid interface: a thermodynamical approach
Surf. Sci.
(2009) - et al.
Kinetics of polymer adsorption in stagnation point flow
Colloids Surface.
(1990) - et al.
Measuring interactions between yeast cells and a micro-sized air bubble via atomic force microscopy
J. Colloid Interface Sci.
(2018) - et al.
Investigation on surface structure of potassium permanganate/nitric acid treated poly(tetrafluoroethylene)
Appl. Surf. Sci.
(2014) - et al.
Role of extracellular polymeric substance in determining the high aggregation ability of anammox sludge
Water Res.
(2015) Direct measurement of hydrophobic particle–bubble interactions in aqueous solutions by atomic force microscopy: effect of particle hydrophobicity
Colloid. Surf. Physicochem. Eng. Asp.
(2007)
Crater formation on anaerobic granular sludge
Chem. Eng. J.
A simple and low cost technique for determining the granulometry of upflow anaerobic sludge blanket reactor sludge
Water Sci. Technol.
Hydrophilicity/hydrophobicity of anaerobic granular sludge surface and their causes: an in situ research
Bioresour. Technol.
Six-helix bundle assembly and analysis of the central core of mumps virus fusion protein
Arch. Biochem. Biophys.
Fabrication of super-hydrophobic film from PMMA with intrinsic water contact angle below 90°
Polymer
Binding characteristics of perylene, phenanthrene and anthracene to different DOM fractions from lake water
J. Environ. Sci.
Hydrodynamic interaction between an air bubble and a particle: atomic force microscopy measurements
Exp. Therm. Fluid Sci.
A study of bubble–particle interaction using atomic force microscopy
Miner. Eng.
A little breath of fresh air into an anaerobic system: how microaeration facilitates anaerobic digestion process
Biotechnol. Adv.
Dispersion and treatment performance analysis of an UASB reactor under different hydraulic loading rates
Water Res.
Investigations of bubble–particle interactions
Int. J. Miner. Process.
Protein extraction from activated sludge: an analytical approach
Water Res.
Evaluation of different types of anaerobic seed sludge for the high rate anaerobic digestion of pig slurry in UASB reactors
Bioresour. Technol.
Deposition of bitumen and asphaltene-stabilized emulsions in an impinging jet cell
J. Colloid Interface Sci.
Extracellular polymeric substances (EPS) of microbial aggregates in biological wastewater treatment systems: a review
Biotechnol. Adv.
What is the role of hydrophilic/hydrophobic surface forces and/or polar interfacial interactions in the interaction between bubbles and minerals?
Colloid. Surf. Physicochem. Eng. Asp.
Sorption properties of biofilms
Water Sci. Technol.
Settling velocity and size distribution measurement of anaerobic granular sludge using microscopic image analysis
J. Microbiol. Methods
CFD simulation of an expanded granular sludge bed (EGSB) reactor for biohydrogen production
Int. J. Hydrogen Energy
Characterising the two-phase flow and mixing performance in a gas-mixed anaerobic digester: importance for scaled-up applications
Water Res.
Understanding the granulation process of activated sludge in a biological phosphorus removal sequencing batch reactor
Chemosphere
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These authors contributed equally.