2019
DOI: 10.3390/en12091586
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Integration of Hydrothermal Carbonisation with Anaerobic Digestion; Opportunities for Valorisation of Digestate

Abstract: Hydrothermal carbonisation (HTC) has been identified as a potential route for digestate enhancement producing a solid hydrochar and a process water rich in organic carbon. This study compares the treatment of four dissimilar digestates from anaerobic digestion (AD) of agricultural residue (AGR); sewage sludge (SS); residual municipal solid waste (MSW), and vegetable, garden, and fruit waste (VGF). HTC experiments were performed at 150, 200 and 250 °C for 1 h using 10%, 20%, and 30% solid loadings of a fixed wa… Show more

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Cited by 102 publications
(81 citation statements)
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“…The HTC residence time, used by Aragón-Briceño et al (30 min) [37], was also much lower in comparison to the residence time in this study (270 min). However, the COD obtained in this study (Table 2) is very close to the one obtained for HTC of an agricultural digestate by Parmar and Ross (between 42.2 and 46.3 g/dm 3 ) [36]. Overall, the spread of COD results presented in the literature, for effluents from HTC of by-products of fermentation processes, is quite wide (17.5 up to 105.6 g/dm 3 ) in itself.…”
Section: Samplesupporting
confidence: 86%
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“…The HTC residence time, used by Aragón-Briceño et al (30 min) [37], was also much lower in comparison to the residence time in this study (270 min). However, the COD obtained in this study (Table 2) is very close to the one obtained for HTC of an agricultural digestate by Parmar and Ross (between 42.2 and 46.3 g/dm 3 ) [36]. Overall, the spread of COD results presented in the literature, for effluents from HTC of by-products of fermentation processes, is quite wide (17.5 up to 105.6 g/dm 3 ) in itself.…”
Section: Samplesupporting
confidence: 86%
“…These compounds were not detected for short residence times [44], which suggests that the reactions responsible for the formation of these compounds are relatively slow, and compounds can be produced in relatively long residence times, which was the case in this study. 3 139.6 Chemical oxygen demand (COD), mg O2/dm 3 31,650 Biochemical oxygen demand (BOD), mg O2/dm 3 9520 Dissolved organic carbon (DOC), mg C/dm 3 15,281 N-NH4 + , mg/dm 3 700 N-NO2 − , mg/dm 3 0.1 N-NO3 − , mg/dm 3 below the limit of detection PO4 3− , mg/dm 3 950 Na, mg/dm 3 293.6 K, mg/dm 3 688.9 Ca, mg/dm 3 28.2 Mg, mg/dm 3 449.7 Cl−, mg/dm 3 85.7 Fe, mg/dm 3 22.13 Mn, mg/dm 3 1.68 Cu, mg/dm 3 0.71 Zn, mg/dm 3 1 It seems to be plausible to state that the liquid, with the content of such compounds, can be utilized effectively in the anaerobic digestion process, thus allowing the integration of the anaerobic digestion with HTC of its wet by-products, as already suggested by some authors [36,37,45]. Further research is needed to confirm this, assessing the influence of adding such a liquid to AD reactors and optimize the process, configured in such way (AD + HTC).…”
Section: Samplementioning
confidence: 86%
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“…Nonetheless, the results obtained with this formula should be regarded as accurate for several reasons. Firstly, the standard error of calibration of 337 kJ/kg and an R 2 coefficient of 0.943 achieved during validation of the against the experimental results [58,69]. Secondly, cereals were used among the materials, used for the validation formula.…”
Section: Resultsmentioning
confidence: 99%
“…Similarly, approximately one third of the original chemical energy of the feedstock is lost to by-products. However, this energy can be recovered by adding this liquid into anaerobic digestion reactors, as suggested by many studies of HTC of different types of biomass [43,69,[90][91][92][93][94][95].…”
Section: Resultsmentioning
confidence: 99%