-
Je něco špatně v tomto záznamu ?
Nitrification in a completely stirred tank reactor treating the liquid phase of digestate: The way towards rational use of nitrogen
P. Svehla, H. Radechovska, L. Pacek, P. Michal, A. Hanc, P. Tlustos,
Jazyk angličtina Země Spojené státy americké
Typ dokumentu časopisecké články
- MeSH
- amoniak MeSH
- bioreaktory * MeSH
- dusík MeSH
- dusitany MeSH
- nitrifikace * MeSH
- Publikační typ
- časopisecké články MeSH
The nitrification of the liquid phase of digestate (LPD) was conducted using a 5L completely stirred tank reactor (CSTR) in two independent periods (P1 - without pH control; P2 - with pH control). The possibility of minimizing nitrogen losses during the application of LPD to the soil as well as during long-term storage or thermal thickening of LPD using nitrification was discussed. Moreover, the feasibility of applying the nitrification of LPD to the production of electron acceptors for biological desulfurization of biogas was assessed. Despite an extremely high average concentration of ammonia and COD in LPD reaching 2470 and 9080mg/L, respectively, nitrification was confirmed immediately after the start-up of the CSTR. N-NO3-concentration reached 250mg/L only two days after the start of P1. On the other hand, P1 demonstrated that working without pH control is a risk because of the free nitrous acid (FNA) inhibition towards nitrite oxidizing bacteria (NOB) resulting in massive nitrite accumulation. Up to 30.9mg/L of FNA was present in the reactor during P1, where the NOB started to be inhibited even at 0.15mg/L of FNA. During P2, the control of pH at 7.0 resulted in nitrogen oxidation efficiency reaching 98.3±1.5% and the presence of N-NO3-among oxidized nitrogen 99.6±0.4%. The representation of volatile free ammonia within total nitrogen was reduced more than 1000 times comparing with raw LPD under these conditions. Thus, optimum characteristics of the tested system from the point of view of minimizing the nitrogen losses as well as production of electron acceptors for the desulfurization of biogas were gained in this phase of reactor operation. Based on the results of the experiments, potential improvements and modifications of the tested system were suggested.
Citace poskytuje Crossref.org
- 000
- 00000naa a2200000 a 4500
- 001
- bmc18010696
- 003
- CZ-PrNML
- 005
- 20180426090252.0
- 007
- ta
- 008
- 180404s2017 xxu f 000 0|eng||
- 009
- AR
- 024 7_
- $a 10.1016/j.wasman.2017.03.041 $2 doi
- 035 __
- $a (PubMed)28385350
- 040 __
- $a ABA008 $b cze $d ABA008 $e AACR2
- 041 0_
- $a eng
- 044 __
- $a xxu
- 100 1_
- $a Svehla, Pavel $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic.
- 245 10
- $a Nitrification in a completely stirred tank reactor treating the liquid phase of digestate: The way towards rational use of nitrogen / $c P. Svehla, H. Radechovska, L. Pacek, P. Michal, A. Hanc, P. Tlustos,
- 520 9_
- $a The nitrification of the liquid phase of digestate (LPD) was conducted using a 5L completely stirred tank reactor (CSTR) in two independent periods (P1 - without pH control; P2 - with pH control). The possibility of minimizing nitrogen losses during the application of LPD to the soil as well as during long-term storage or thermal thickening of LPD using nitrification was discussed. Moreover, the feasibility of applying the nitrification of LPD to the production of electron acceptors for biological desulfurization of biogas was assessed. Despite an extremely high average concentration of ammonia and COD in LPD reaching 2470 and 9080mg/L, respectively, nitrification was confirmed immediately after the start-up of the CSTR. N-NO3-concentration reached 250mg/L only two days after the start of P1. On the other hand, P1 demonstrated that working without pH control is a risk because of the free nitrous acid (FNA) inhibition towards nitrite oxidizing bacteria (NOB) resulting in massive nitrite accumulation. Up to 30.9mg/L of FNA was present in the reactor during P1, where the NOB started to be inhibited even at 0.15mg/L of FNA. During P2, the control of pH at 7.0 resulted in nitrogen oxidation efficiency reaching 98.3±1.5% and the presence of N-NO3-among oxidized nitrogen 99.6±0.4%. The representation of volatile free ammonia within total nitrogen was reduced more than 1000 times comparing with raw LPD under these conditions. Thus, optimum characteristics of the tested system from the point of view of minimizing the nitrogen losses as well as production of electron acceptors for the desulfurization of biogas were gained in this phase of reactor operation. Based on the results of the experiments, potential improvements and modifications of the tested system were suggested.
- 650 _2
- $a amoniak $7 D000641
- 650 12
- $a bioreaktory $7 D019149
- 650 12
- $a nitrifikace $7 D058465
- 650 _2
- $a dusitany $7 D009573
- 650 _2
- $a dusík $7 D009584
- 655 _2
- $a časopisecké články $7 D016428
- 700 1_
- $a Radechovska, Helena $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic.
- 700 1_
- $a Pacek, Lukas $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic.
- 700 1_
- $a Michal, Pavel $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic. Electronic address: michalp@af.czu.cz.
- 700 1_
- $a Hanc, Ales $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic.
- 700 1_
- $a Tlustos, Pavel $u Department of Agro-Environmental Chemistry and Plant Nutrition, Czech University of Life Sciences Prague, Kamycka 129, Prague 165 21, Czech Republic.
- 773 0_
- $w MED00006459 $t Waste management (New York, N.Y.) $x 1879-2456 $g Roč. 64, č. - (2017), s. 96-106
- 856 41
- $u https://pubmed.ncbi.nlm.nih.gov/28385350 $y Pubmed
- 910 __
- $a ABA008 $b sig $c sign $y a $z 0
- 990 __
- $a 20180404 $b ABA008
- 991 __
- $a 20180426090402 $b ABA008
- 999 __
- $a ok $b bmc $g 1288181 $s 1007508
- BAS __
- $a 3
- BAS __
- $a PreBMC
- BMC __
- $a 2017 $b 64 $c - $d 96-106 $e 20170403 $i 1879-2456 $m Waste management $n Waste Manag $x MED00006459
- LZP __
- $a Pubmed-20180404