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Methane production during laboratory-scale co-digestion of cattle slurry with 10 wt. % of various biowastes

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EN
Abstrakty
EN
The paper summarizes the results from twenty model tests of continuous one-stage mesophilic anaerobic co-digestion of cattle slurry (90 wt. %) and various biowastes (10 wt. %). Digestion was conducted in 0.06 m3 reactors with hydraulic retention times ranging from 60 to 98 days during the research period 2007-2010. Methane production intensity and specific methane production are discussed. The highest methane production intensity (0.85 mN3.m-3.d-1) was from a mixture of 63 wt. % of total solids from biscuit meal EKPO - EB and from 37 wt. % of total solids from cattle slurry. The highest specific methane production from 1 kg of added organic compounds (0.67 mN3.kgVSp-1) was given by a mixture containing 61 wt. % of total solids using spring barley Aksamit (milled grain) and 39 wt. % of total solids from cattle slurry. The highest substrate-specific methane production (0.92 mN3.kgVSp-1) was from milled grains of winter rye Aventino.
Rocznik
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14--20
Opis fizyczny
Bibliogr. 13 poz., rys., tab.
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autor
autor
autor
Bibliografia
  • 1. El-Mashad, H.M. & Ruihong, Z. (2010) Biogas production from co-digestion of dairy manure and food waste. Bioresource Technology, 101 (11), 4021–4028. DOI: 10.1016/j.biortech.2010.01.027.
  • 2. Murto, M., Bjornsson, L. & Mattiasson, B. (2004) Impact of food industrial waste on anaerobic co-digestion of sewage sludge and pig manure. Journal of Environmental Management. 70 (2), 101–107. DOI:10.1016/j.jenvman.2003.11.001.
  • 3. Callaghan, F.J., Wase, D.A.J., Thayanithy, K. & Forster, C.F. (1999) Co-digestion of waste organic solids: Batch studies. Bioresource Technology. 67 (2), 117–122. DOI: 10.1016/S0960- 8524(98)00108-4.
  • 4. Demirer G.N. & Chen, S. (2005) Anaerobic digestion of dairy manure in a hybrid reactor with biogas recirculation. World Journal of Microbiology & Biotechnology. 21 (8–9), 1509–1514. DOI: 10.1007/s11274-005-7371-6.
  • 5. Ahring, B.K., Ibrahim A.A. & Mladenovska, Z. (2001) Effect of temperature increase from 55 to 65 °C on performance and microbial population dynamics of an anaerobic reactor treating cattle manure. Water Research, 35 (10), 2446–2452, DOI: 10.1016/S0043-1354(00)00526-1.
  • 6. Chen, Y.R. (1983) Biogas digester design. Fuel Gas Systems, Ser. Bioenergy Systems, 23–59, CRC Press Inc., Boca Raton, Fl. USA.
  • 7. Habig, C. & Ryther, J.H. (1984) Some correlations between substrate compositions and biogas yields. Proc. Syp. IGT Energy from Biomass and Waste 8th, 30.1.-3.2. 1984. (pp. 817–832). Lake Buena Vista, FA, USA.
  • 8. Straka, F., Kunčarová, M. & Lacek, P. (2007) Optimization of load types for biogas station using biomass, animal wastes or other possible animal products. Praha. GAS s.r.o. /in Czech/.
  • 9. Straka, F., Dohányos, M., Zábranská, J., Jeníček, P., Dědek, J., Malijevský, A., Novák, J., Oldřich, J. & Kunčarová, M. (2006). Biogas – a handbook for teaching, design and operation of biogas systéme (2nd ed.), GAS s.r.o. Praha /in Czech/.
  • 10. Selly, R.J. (1983) Comparative Anaerobic Digestion of Organic Residues. Ser. Bioenergy Systems, 157–170, CRC Press Inc., Boca Raton, Fl. USA.
  • 11. Das, D. a sp. (1983) Treatment of distillery waste by a two phase biomethanation process, Proc. Syp. IGT Energy from Biomass and Waste 7th, 1–3 February 1983 (pp. 601–626). Lake Buena Vista, FA,USA.
  • 12. Sales, D. Valcarcel, M.J. & Romero, L.I. (1989) Anaerobic digestion kinetics of wine-destilleries wastewaters, J. Chem. Tech. Biotechnology. 45 (2), 147–162. DOI: 10.1002/jctb.280450208.
  • 13. Holder, D. (2000) Anaerobic digestion for heat, cold power generation. Proceedings of the Conference biomass renewable energy source in the landscape, 5–6 October 2010 (pp.115–118),Průhonice, ČR. /in Czech.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS2-0064-0036
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