Prerequisite – An electrohydrolysis pretreatment for anaerobic digestion of lignocellulose waste material
Graphical abstract
Schematic diagram of electrohydrolysis pretreatment of anaerobic digestion of lignocellulose waste material.
Introduction
An anaerobic digestion is a mature technology widely applied for bioenergy production from the sewage sludge, animal manure, agricultural residue, industrial sludge and energy crops in developing and developed countries (Li and Khanal, 2016). These substrate has high levels of biodegradable organics make it an ideal feedstock for anaerobic digestion. Due to the continuous production in the industrial level, there is a huge accumulation of waste especially in pulp and paper mill industry, the gargantuan quantity of sludge was produced. Handling and management of this produced sludge from effluent treatment plant of pulp and paper mill has account more than 60% of the total wastewater treatment plant operating cost (Monte et al., 2009, Xu and Lancaster, 2009). Jackson et al. (2000) reported the produced sludge contains 45–50% of organic fraction with high moisture content that can be treated efficiently by biological treatment than thermal treatment.
The lignocellulose material consists mainly of cellulose, hemicellulose, and lignin. Due to the inherent recalcitrant structure of lignocellulose material towards enzymatic deconstruction (Himmel et al., 2007) pretreatment is necessary to make the holocelluloses amenable to enzymatic hydrolysis and fermentation (Yang and Wyman, 2008, Sharma et al., 2015). In recent years there has been renewed interest in pretreatment of lignocellulose biomass and waste for anaerobic digestion. The several structural and compositional properties of lignocellulosic content render it resistant to biodegradation. Even though there has been an extensive research on the effect of pretreatment, the correlation between the degradability of lignocellulose material, the structural and compositional properties remains unclear and contradictory (Zheng et al., 2014). Different kinds of physical, chemical, and biological pretreatments have been proposed for the conversion of organic matter to valuable energy source as biogas (Elliott and Mahmood, 2007).
As hydrolysis is a rate-limiting step in anaerobic digestion of pulp and paper mill sludge (PPMS) (Elliott and Mahmood, 2012, Wood et al., 2009) and also in previous study by Veluchamy and Kalamdhad (2017) reported that pretreatment is necessary to fasten the hydrolysis stage because of the longer digestion time. To accelerate the hydrolysis step, a novel electrohydrolysis pretreatment was investigated. Based on literature known so for, an electrohydrolysis pretreatment has been studied first to improve the hydrolysis stage in anaerobic digestion of lignocellulose waste material. The principle of electrohydrolysis pretreatment relies on electrophoresis, ohmic heating and electroosmosis resulting in the disintegration of particles and microbial cell lysis (Zhen et al., 2014). The electrophoresis is the process in which shifting of ions relative to a static phase depending on its electrical charge and molecular size (Mahmoud et al., 2010). The process in which thermal energy is generated by passing electric current through organic materials is known as ohmic heating (Varghese et al., 2014). The motion of solid particles suspended in a liquid, under the influence of an electrical field is known as electro-osmosis (Mahmoud et al., 2010). Electrohydrolysis is the process of passing direct current (DC) through an ionic substance to solubilize the organic matter by breaking the bonds between polymers induced by application of current through electrodes. Electrodes when connected to DC one becomes positively charged electrode and another becomes negatively charged electrode. This initiates the movement of electrolyte towards electrodes i.e., positive ions move to cathode and negative ions move to anode.
To delineate the effect of electrohydrolysis pretreatment, an applied voltage (DC) and time study were performed to fasten the hydrolysis step in anaerobic digestion. Therefore, in the light of literature studies the objective of this study is to the investigate the effect of electrohydrolysis pretreatment conditions (applied voltage and time), also to elucidate the changes produced in the structure and composition of the PPMS before and after pretreatment, followed by the batch anaerobic digestion process for the biological conversion of PPMS into biogas.
Section snippets
Materials
PPMS was obtained from the Nagaon paper mill located at Jagiroad, Assam, India. PPMS collected from the filter house of effluent treatment plant was used as a substrate. Collected PPMS was stored in refrigerator at 4 °C before further use. Cow dung collected from farm present in the vicinity of Indian Institute of Technology Guwahati, North Guwahati, India, was used as the inoculum for the batch study. Table 1 shows the initial chemical characterization of substrate and inoculum.
Experimental set up
Fig. 1 gives the
Effect of sCOD and VFA with applied voltage
The effect of applied voltage with constant time on PPMS treated by DC current in electrohydrolysis pretreatment was shown in Fig 2(a). It was observed from the Fig 2(a) that the increase in applied voltage has shown increase in solubilization rate which was measured in the form of sCOD and VFA. The sCOD and VFA increased up to 15 V and then it got reduced. Further increasing the applied voltage shows decrease in sCOD and VFA. At higher applied voltage, there is a release of higher quantity of
Conclusion
The novel study revealed that electrohydrolysis pretreatment has significant effect on lignocellulose content in speedup the hydrolysis step in anaerobic digestion process. It was perceived that the organic and inorganic compounds were efficiently solubilized at 15 V for 45 min in electrohydrolysis pretreatment. Compositional and instrumental analysis such as FESEM, XRD, and FT-IR spectra showed that the electrohydrolysis pretreatment has strongly affect the lignocellulose structures. Batch study
Acknowledgement
The authors would like to thank Dr. Praveen Kumar, Department of Electronics and Electrical Engineering, Indian Institute of Technology Guwahati, for providing the laboratory facility.
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