Elsevier

Bioresource Technology

Volume 276, March 2019, Pages 97-102
Bioresource Technology

Hydrogen enrichment as a bioaugmentation tool to alleviate ammonia inhibition on anaerobic digestion of phenol-containing wastewater

https://doi.org/10.1016/j.biortech.2018.12.099Get rights and content

Highlights

  • The endurance to ammonia toxicity of sludge was enhanced by hydrogen enrichment.

  • Phenol degradation and methanogenic activity were improved with the increase of HPP.

  • Syntrophic interactions were well established under high ammonia concentration.

  • Three hydrogen-consuming pathways were simulated by hydrogen enrichment.

Abstract

Phenol and ammonia are prevalent toxic pollutants in various industrial wastewaters, but phenol degraders are frequently inhibited by high concentration of ammonia. Hydrogen enrichment was developed to alleviate ammonia inhibition on anaerobic digestion of phenol-containing wastewater. Results indicated that the endurance to ammonia of sludge was improved greatly by hydrogen enrichment at higher ammonia concentration (from 2 to 8 g NH4+-N/L) compared with the control group. Furthermore, phenol utilization rate of sludge was gradually enhanced with the increase of initial hydrogen partial pressure (HPP) at ammonia concentration of 2 g NH4+-N/L and the maximum rate of 199.75 mg/g VSS/d was achieved under 0.8 atm HPP. The maximum SMA of acetate and hydrogen was 0.61 and 0.45 g COD-CH4/g VSS/d, respectively under 0.8 atm HPP. Three hydrogen-consuming pathways including homoacetogenesis, hydrogenotrophic methanogenesis and benzoate generation played the critical roles in enhancing anaerobic digestion of phenol by hydrogen enrichment under high ammonia concentration.

Introduction

There are various industrial wastewaters containing extremely high concentration of phenolic compounds and ammonia, such as coal gasification wastewater, coking wastewater, and petrochemical wastewater (Rosenkranz et al., 2013, Wang et al., 2012). As the major pollutants of these wastewaters, the concentration of phenolic compounds and ammonia can even exceed over 4000 and 3000 mg/L, respectively (Gai et al., 2008). The development of technique to achieve the harmlessness and energy recovery of phenolic compounds is still quite urgent. Anaerobic digestion is regarded as a technical feasible and economically attractive strategy of phenol-containing wastewater treatment (Na et al., 2016, Rosenkranz et al., 2013), but phenol degraders are easily inhibited by the high concentration of ammonia (Wang et al., 2017b). Therefore, developing an efficient way is necessary to enhance anaerobic digestion of phenol under high ammonia concentration condition.

Interestingly, hydrogen enrichment is used as a tool for in-situ biogas upgrading, as hydrogen introduced into the anaerobic digester can be converted together with carbon dioxide into methane by hydrogenotrophic methanogens (Luo et al., 2012). Meanwhile, hydrogen enrichment is considered a great way to enhance the hydrogenotrophic methanogenic activity of sludge, and the increase of relative abundance of hydrogenotrophic methanogens occurs during this process (Luo and Angelidaki, 2012). Hydrogenotrophic methanogens are more tolerant to ammonia and phenol toxicity compared with acetoclastic methanogens (Wang et al., 2016, Yenigun and Demirel, 2013). Importantly, the syntrophic conversion of phenol to methane was proposed only favorable via the hydrogenotrophic pathway at high inhibitory levels (Poirier et al., 2016a). The well-established syntrophic interactions between syntrophs and hydrogen consuming microorganisms (i.e. methanogens or homoacetogens) can accelerate finial conversion of phenol (Karlsson et al., 2000). Nevertheless, the rate-limiting step of anaerobic phenol degradation is reduction to benzoate (Veeresh et al., 2005). High hydrogen partial pressure (HPP) can suppress degradation of benzoate thermodynamically (Zhuang et al., 2015). Therefore, it is not clear whether hydrogen enrichment can be used as a bioaugmentation tool to enhance anaerobic digestion of phenol under high ammonia concentration.

The aims of this study were to investigate the effect of hydrogen enrichment on anaerobic digestion of phenol under high ammonia concentration condition, and to discuss the influencing factors and potential mechanisms of hydrogen enrichment on phenol degradation and methane production. Furthermore, more insights were given into the shift and mechanism of microbial community occurring in response to hydrogen enrichment.

Section snippets

Inoculum and wastewater composition

Anaerobic granular sludge obtained from an UASB reactor treating phenolic wastewater was used as the inoculum (Wang et al., 2017c). The total suspended sludge (TSS) of seed sludge was 50.91 g/L and the ratio of volatile suspended sludge (VSS) and TSS was 0.80. Phenol was used as the sole carbon resource in the medium, and the concentration of phenol was set at 1000 mg/L in all batch tests. Ammonium chloride was used as ammonia source. The macronutrients and micronutrients in the medium were

Impact of hydrogen enrichment on anaerobic digestion of phenol under high ammonia concentrations

The impact of hydrogen enrichment on phenol removal efficiency under different ammonia concentrations is shown in Fig. 1. When the concentration of ammonia was increased from 2 to 4 g NH4+-N/L, the corresponding phenol removal efficiency of the control group was significantly decreased from 41.38% to 8.49% (P = 3.0 × 10−5 < 0.05). Furthermore, when the sludge was exposed to 6 and 8 g NH4+-N/L, the phenol degradation in the control group tended to be completely inhibited, and the corresponding

Conclusion

Hydrogen enrichment was successfully developed to alleviate ammonia inhibition on anaerobic digestion of phenol. The endurance to ammonia toxicity of sludge was greatly enhanced by introducing hydrogen under high ammonia levels (from 2 to 8 g NH4+-N/L). Phenol utilization rate, the acetoclastic and hydrogenotrophic methanogenic activities of sludge were gradually improved with the increase of initial HPP at high ammonia concentration. Moreover, three hydrogen-consuming pathways including

Acknowledgements

This work was supported by the National Natural Science Foundation of China (51878232) and CAS Key Laboratory of Urban Pollutant Conversion, University of Science and Technology of China (KF201702).

References (36)

  • B.K. Acharya et al.

    Kinetic modelling and microbial community assessment of anaerobic biphasic fixed film bioreactor treating distillery spent wash

    Water Res.

    (2011)
  • APHA

    Standard Methods for the Examination of Water and Wastewater

    (2005)
  • C.L. Chen et al.

    Identification of important microbial populations in the mesophilic and thermophilic phenol-degrading methanogenic consortia

    Water Res.

    (2008)
  • S. Fujishima et al.

    Effect of moisture content on anaerobic digestion of dewatered sludge: ammonia inhibition to carbohydrate removal and methane production

    Water Sci. Technol.

    (2000)
  • H. Gai et al.

    Conceptual design and retrofitting of the coal-gasification wastewater treatment process

    Chem. Eng. J.

    (2008)
  • S.M. Gao et al.

    Tolerance response to in situ ammonia stress in a pilot-scale anaerobic digestion reactor for alleviating ammonia inhibition

    Bioresour. Technol.

    (2015)
  • F. Ju et al.

    Novel microbial populations in ambient and mesophilic biogas-producing and phenol-degrading consortia unraveled by high-throughput sequencing

    Microbial Ecol.

    (2014)
  • S.V. Kalyuzhnyi et al.

    Organic removal and microbiological features of UASB-reactor under various organic loading rates

    Bioresour. Technol.

    (1996)
  • A. Karlsson et al.

    CO2-dependent fermentation of phenol to acetate, butyrate and benzoate by an anaerobic, pasteurised culture

    Arch. Microbiol.

    (2000)
  • L. Leven et al.

    Conversion of phenols during anaerobic digestion of organic solid waste – a review of important microorganisms and impact of temperature

    J. Environ. Manage.

    (2012)
  • B. Liang et al.

    Anaerolineaceae and Methanosaeta turned to be the dominant microorganisms in alkanes-dependent methanogenic culture after long-term of incubation

    Amb Express

    (2015)
  • M.M. Liu et al.

    Impacts of biostimulation and bioaugmentation on the performance and microbial ecology in methanogenic reactors treating purified terephthalic acid wastewater

    Water Res.

    (2017)
  • G. Luo et al.

    Hollow fiber membrane based H2 diffusion for efficient in situ biogas upgrading in an anaerobic reactor

    Appl. Microbiol. Biotechnol.

    (2013)
  • G. Luo et al.

    Integrated biogas upgrading and hydrogen utilization in an anaerobic reactor containing enriched hydrogenotrophic methanogenic culture

    Biotechnol. Bioeng.

    (2012)
  • G. Luo et al.

    Simultaneous hydrogen utilization and in situ biogas upgrading in an anaerobic reactor

    Biotechnol. Bioeng.

    (2012)
  • J.G. Na et al.

    Microbial community analysis of anaerobic granules in phenol-degrading UASB by next generation sequencing

    Biochem. Eng. J.

    (2016)
  • B. Omar et al.

    Simultaneous biogas upgrading and biochemicals production using anaerobic bacterial mixed cultures

    Water Res.

    (2018)
  • S. Poirier et al.

    Community shifts within anaerobic digestion microbiota facing phenol inhibition: towards early warning microbial indicators?

    Water Res.

    (2016)
  • Cited by (0)

    View full text