2014
DOI: 10.1016/j.bej.2014.01.001
|View full text |Cite
|
Sign up to set email alerts
|

Two-stage CSTR–UASB digestion enables superior and alkali addition-free cheese whey treatment

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
27
0
3

Year Published

2014
2014
2024
2024

Publication Types

Select...
7

Relationship

1
6

Authors

Journals

citations
Cited by 47 publications
(32 citation statements)
references
References 34 publications
1
27
0
3
Order By: Relevance
“…In the only such study found to date, Kim et al (2008) reported lactate and ethanol as the main metabolic products of cheese whey fermentation. Despite the high production of propionate (Table 1), the biogas production rate in the UASB reactor was equal to 4.31 ± 0.53 L L −1 day −1 as the result of the enhanced acidification strategy followed and the two-stage configuration used (Diamantis et al 2014).…”
Section: Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…In the only such study found to date, Kim et al (2008) reported lactate and ethanol as the main metabolic products of cheese whey fermentation. Despite the high production of propionate (Table 1), the biogas production rate in the UASB reactor was equal to 4.31 ± 0.53 L L −1 day −1 as the result of the enhanced acidification strategy followed and the two-stage configuration used (Diamantis et al 2014).…”
Section: Discussionmentioning
confidence: 99%
“…The system consisted of an acidogenic CSTR accompanied with a clarifier for biomass settlement and a methanogenic UASB reactor (Diamantis et al 2014). The CSTR was initially filled with biomass which had spontaneously developed in a tank used for long-term cheese whey storage, whereas the UASB reactor was fed with granular sludge obtained from the cheese whey factory.…”
Section: Methodsmentioning
confidence: 99%
“…Empleando un sistema compuesto por dos reactores tipo CSTR, que incorpora una unidad de filtración de membrana para la recirculación en la segunda etapa, se consiguió operar con cargas de hasta 19,8gDQO/Ld con un eliminación de DQO del 79% [84]. Diamantis et al [85], evaluaron un sistema de dos fases compuesto de un reactor CSTR para la acidificación, seguido de un reactor UASB para la metanización. Estos autores alcanzaron conversiones de biomasa de hasta un 90% con rendimientos de producción de metano de 0,37m 3 CH 4 /kgDQOeliminado.…”
Section: Producción De Hidrógenounclassified
“…Diamantis et al [24] developed a two-stage CSTR-UASB system without any requirements for alkali consumption for the anaerobic treatment of diluted cheese whey with dairy-washing waters.…”
Section: Introductionmentioning
confidence: 99%
“…In this regard Spachos and Stamatis [14] performed an exergetic and economic analysis of an anaerobic treatment system of whey accompanied by the production of steam, concluding that the anaerobic treatment of whey can be a sustainable investment, at least for a substantial volume of whey. The anaerobic treatment of cheese whey has been well reported by several authors under different systems and conditions, mainly in high-rate anaerobic systems, such as the upflow anaerobic sludge blanket (UASB) reactor [11,[15][16][17][18][19][20][21][22][23][24].…”
Section: Introductionmentioning
confidence: 99%