Research article

Evaluating the level of ammonia and sulfide in the liquid phase during anaerobic digestion of slaughterhouse waste operating at mesophilic scale digester—the impact of inhibition and process performance

  • Received: 19 April 2020 Accepted: 21 June 2020 Published: 10 July 2020
  • The performance of experimental batch-reactor loaded with slaughterhouse waste at mesophilic temperature was investigated as well as the inhibition of both ammonia and sulfide concentration in the aqueous phase. The digester was operated for 68 days by evaluating the process stability basing on controlling parameters such as pH, volatile fatty acids and alkalinity in relation to the methane produced. The maximum CH4 content of 69.6% was achieved at 0.37 VFA/Alkalinity ratio and pH of 7.51 during day 37 of anaerobic digestion. However, a sudden increase of ammonia nitrogen in the digester from day 44 to day 68 decreased the methane content about 62.15% from 65% to 24.6%. Similarly, as the amount of sulfide content decreased in the liquid phase, gaseous H2S was elevated up to 132 ppm in the 68th day. During this time, it was observed that the ratio of VFA/Alkalinity decreased to 0.16, with a very low concentration of VFA, which was 150.92 mg/L. This phenomenon indicated that all the acids produced were consumed by methanogens and ammonia inhibition was at the highest rate due to the increase of ammonia nitrogen concentration in the last days of digestion. Furthermore, among of peculiar characteristic shown by slaughterhouse waste is the ability to maintain the pH above 7 without the addition of any buffering agent throughout the AD process. Meanwhile, the evaluation of the level of both ammonia and sulfide in the aqueous phase revealed that the inhibitory effect of ammonia concentration was higher than sulfide concentration.

    Citation: Eric Mutegoa, Isack Kandola, Askwar Hilonga, Karoli N. Njau. Evaluating the level of ammonia and sulfide in the liquid phase during anaerobic digestion of slaughterhouse waste operating at mesophilic scale digester—the impact of inhibition and process performance[J]. AIMS Energy, 2020, 8(4): 615-626. doi: 10.3934/energy.2020.4.615

    Related Papers:

  • The performance of experimental batch-reactor loaded with slaughterhouse waste at mesophilic temperature was investigated as well as the inhibition of both ammonia and sulfide concentration in the aqueous phase. The digester was operated for 68 days by evaluating the process stability basing on controlling parameters such as pH, volatile fatty acids and alkalinity in relation to the methane produced. The maximum CH4 content of 69.6% was achieved at 0.37 VFA/Alkalinity ratio and pH of 7.51 during day 37 of anaerobic digestion. However, a sudden increase of ammonia nitrogen in the digester from day 44 to day 68 decreased the methane content about 62.15% from 65% to 24.6%. Similarly, as the amount of sulfide content decreased in the liquid phase, gaseous H2S was elevated up to 132 ppm in the 68th day. During this time, it was observed that the ratio of VFA/Alkalinity decreased to 0.16, with a very low concentration of VFA, which was 150.92 mg/L. This phenomenon indicated that all the acids produced were consumed by methanogens and ammonia inhibition was at the highest rate due to the increase of ammonia nitrogen concentration in the last days of digestion. Furthermore, among of peculiar characteristic shown by slaughterhouse waste is the ability to maintain the pH above 7 without the addition of any buffering agent throughout the AD process. Meanwhile, the evaluation of the level of both ammonia and sulfide in the aqueous phase revealed that the inhibitory effect of ammonia concentration was higher than sulfide concentration.


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    [1] Afazeli H, Jafari A, Rafiee S, et al. (2014) An investigation of biogas production potential from livestock and slaughterhouse wastes. Renewable Sustainable Energy Rev 34: 380-386. doi: 10.1016/j.rser.2014.03.016
    [2] Shen F, Yuan H, Pang Y, et al. (2013) Performances of anaerobic co-digestion of fruit & vegetable waste (FVW) and food waste (FW): single-phase vs. two-phase. Bioresour Technol 144: 80-85. doi: 10.1016/j.biortech.2013.06.099
    [3] Jena S, Mishra S, Acharya S, et al. (2017) An experimental approach to produce biogas from semi dried banana leaves. Sustainable Energy Technol Assess 19: 173-178. doi: 10.1016/j.seta.2017.01.001
    [4] Zhou S, Zhang Y, Dong Y (2012) Pretreatment for biogas production by anaerobic fermentation of mixed corn stover and cow dung. Energy 46: 644-648. doi: 10.1016/j.energy.2012.07.017
    [5] Alfa I, Dahunsi S, Iorhemen O, et al. (2014) Comparative evaluation of biogas production from poultry droppings, cow dung and lemon grass. Bioresour Technol 157: 270-277. doi: 10.1016/j.biortech.2014.01.108
    [6] Lallai A, Mura G, Onnis N (2002) The effects of certain antibiotics on biogas production in the anaerobic digestion of pig waste slurry. Bioresour Technol 82: 205-208. doi: 10.1016/S0960-8524(01)00162-6
    [7] Abubaker J, Risberg K, Jönsson E, et al. (2015) Short-term effects of biogas digestates and pig slurry application on soil microbial activity. Appl Environ Soil Sci 2015.
    [8] Salminen E, Rintala J (2002) Anaerobic digestion of organic solid poultry slaughterhouse waste-A review. Bioresour Technol 83: 13-26. doi: 10.1016/S0960-8524(01)00199-7
    [9] Alvarez R, Liden G (2008) Semi-continuous co-digestion of solid slaughterhouse waste, manure, and fruit and vegetable waste. Renewable Energy 33: 726-734. doi: 10.1016/j.renene.2007.05.001
    [10] Zupančič GD, Jemec A (2010) Anaerobic digestion of tannery waste: semi-continuous and anaerobic sequencing batch reactor processes. Bioresour Technol 101: 26-33. doi: 10.1016/j.biortech.2009.07.028
    [11] Connaughton S, Collins G, O'Flaherty V (2006) Psychrophilic and mesophilic anaerobic digestion of brewery effluent: a comparative study. Water Res 40: 2503-2510. doi: 10.1016/j.watres.2006.04.044
    [12] Banks CJ, Chesshire M, Heaven S, et al. (2011) Anaerobic digestion of source-segregated domestic food waste: performance assessment by mass and energy balance. Bioresour Technol 102: 612-620. doi: 10.1016/j.biortech.2010.08.005
    [13] Ware A, Power N (2016) Biogas from cattle slaughterhouse waste: Energy recovery towards an energy self-sufficient industry in Ireland. Renewable Energy 97: 541-549. doi: 10.1016/j.renene.2016.05.068
    [14] Wirtz M, Droux M (2005) Synthesis of the sulfur amino acids: cysteine and methionine. Photosynth Res 86: 345-362. doi: 10.1007/s11120-005-8810-9
    [15] Lauterböck B, Nikolausz M, Lv Z, et al. (2014) Improvement of anaerobic digestion performance by continuous nitrogen removal with a membrane contactor treating a substrate rich in ammonia and sulfide. Bioresour Technol 158: 209-216. doi: 10.1016/j.biortech.2014.02.012
    [16] Bayr S, Rantanen M, Kaparaju P, et al. (2012) Mesophilic and thermophilic anaerobic co-digestion of rendering plant and slaughterhouse wastes. Bioresour Technol 104: 28-36. doi: 10.1016/j.biortech.2011.09.104
    [17] Bwatota S, Makungu M, Nonga H (2018) Occurrences of indigestible foreign bodies in cattle slaughtered at Morogoro Municipal Slaughterhouse, Tanzania. J Vet Med, 2018.
    [18] Hansen KH, Angelidaki I, Ahring BK (1999) Improving thermophilic anaerobic digestion of swine manure. Water Res 33: 1805-1810. doi: 10.1016/S0043-1354(98)00410-2
    [19] Apha A (2015) Standard Methods for examination of water and wastewater, 22nd Ed, Washington: American Public Health Association, 1360.
    [20] Grimberg S, Hilderbrandt D, Kinnunen M, et al. (2015) Anaerobic digestion of food waste through the operation of a mesophilic two-phase pilot scale digester-assessment of variable loadings on system performance. Bioresour Technol 178: 226-229. doi: 10.1016/j.biortech.2014.09.001
    [21] Mota V, Santos F, Araújo T, et al. (2015) Evaluation of titration methods for volatile fatty acids measurement: effect of the bicarbonate interference and feasibility for the monitoring of anaerobic reactors. Water Pract Technol 10: 486-495. doi: 10.2166/wpt.2015.056
    [22] Harwood J, Kühn A (1970) A colorimetric method for ammonia in natural waters. Water Res 4: 805-811. doi: 10.1016/0043-1354(70)90037-0
    [23] Strocchi A, Furne JK, Levitt MD (1992) A modification of the methylene blue method to measure bacterial sulfide production in feces. J Microbiol Methods 15: 75-82. doi: 10.1016/0167-7012(92)90071-B
    [24] Richard EN, Hilonga A, Machunda RL, et al. (2019) A review on strategies to optimize metabolic stages of anaerobic digestion of municipal solid wastes towards enhanced resources recovery. Sustainable Environ Res 29: 36. doi: 10.1186/s42834-019-0037-0
    [25] Li H, Guo X, Cao F, et al. (2014) Process evolution of dry anaerobic co-digestion of cattle manure with kitchen waste. Chem Biochem Eng Q 28: 161-166.
    [26] Hu J, Zhao J, Wang D, et al. (2018) Effect of diclofenac on the production of volatile fatty acids from anaerobic fermentation of waste activated sludge. Bioresour Technol 254: 7-15. doi: 10.1016/j.biortech.2018.01.059
    [27] Zhang W, Wu S, Guo J, et al. (2015) Performance and kinetic evaluation of semi-continuously fed anaerobic digesters treating food waste: role of trace elements. Bioresour Technol 178: 297-305. doi: 10.1016/j.biortech.2014.08.046
    [28] Ravindranath E, Kalyanaraman C, Begum SS, et al. (2010) Effect of recirculation rate on anaerobic treatment of fleshing using UASB reactor with recovery of energy.
    [29] Paschal C, Gastory L, Katima J, et al. (2017) Application of up-flow anaerobic sludge blanket reactor integrated with constructed wetland for treatment of banana winery effluent. Water Pract Technol 12: 667-674. doi: 10.2166/wpt.2017.062
    [30] Rajagopal R, Massé DI, Singh G (2013) A critical review on inhibition of anaerobic digestion process by excess ammonia. Bioresour Technol 143: 632-641. doi: 10.1016/j.biortech.2013.06.030
    [31] Hansen KH, Angelidaki I, Ahring BK (1998) Anaerobic digestion of swine manure: inhibition by ammonia. Water Res 32: 5-12. doi: 10.1016/S0043-1354(97)00201-7
    [32] Nysing IR, Kramers IH (1958) Absorption of CO2 in carbonate bicarbonate buffer solutions in a wetted wall column. Chem Eng Sci 8: 81-89. doi: 10.1016/0009-2509(58)80039-1
    [33] Haider MR, Yousaf S, Malik RN, et al. (2015) Effect of mixing ratio of food waste and rice husk co-digestion and substrate to inoculum ratio on biogas production. Bioresour Technol 190: 451-457. doi: 10.1016/j.biortech.2015.02.105
    [34] Stefanie JOE, Visser A, Pol LWH, et al. (1994) Sulfate reduction in methanogenic bioreactors. FEMS Microbiol Rev 15: 119-136. doi: 10.1111/j.1574-6976.1994.tb00130.x
    [35] Liu T, Sung S (2002) Ammonia inhibition on thermophilic aceticlastic methanogens. Water Sci Technol 45: 113-120.
    [36] Lauterböck B, Ortner M, Haider R, et al. (2012) Counteracting ammonia inhibition in anaerobic digestion by removal with a hollow fiber membrane contactor. Water Res 46: 4861-4869. doi: 10.1016/j.watres.2012.05.022
    [37] Kayhanian M (1994) Performance of a high‐solids anaerobic digestion process under various ammonia concentrations. J Chem Technol Biotechnol 59: 349-352. doi: 10.1002/jctb.280590406
    [38] Hao L, Mazéas L, Lü F, et al. (2017) Effect of ammonia on methane production pathways and reaction rates in acetate-fed biogas processes. Water Sci Technol 75: 1839-1848. doi: 10.2166/wst.2017.032
    [39] Park J-H, Yoon J-J, Kumar G, et al. (2018) Effects of acclimation and pH on ammonia inhibition for mesophilic methanogenic microflora. Waste Manage 80: 218-223. doi: 10.1016/j.wasman.2018.09.016
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