1994
DOI: 10.1016/0376-7388(94)80040-5
|View full text |Cite
|
Sign up to set email alerts
|

Application of ceramic membrane as a pretreatment in anaerobic digestion of alcohol-distillery wastes

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2
1

Citation Types

1
14
0
1

Year Published

2006
2006
2022
2022

Publication Types

Select...
4
3
1

Relationship

0
8

Authors

Journals

citations
Cited by 57 publications
(16 citation statements)
references
References 8 publications
1
14
0
1
Order By: Relevance
“…This low membrane fouling phenomenon for 1 and 2 kDa membranes was probably the result of a favorable relationship between CFV, pore size and rejected matter. As reported, [17] particles rejected by small pore size membranes could roll off under the forces generated by cross-flow, therefore, not causing membrane blockage. In the case of 500 kDa membrane, flux decline is most probably the result of particles migration through the pores, subsequent adsorption causing enhanced pore blockage or plugging.…”
Section: Membrane Characterizationsupporting
confidence: 51%
See 2 more Smart Citations
“…This low membrane fouling phenomenon for 1 and 2 kDa membranes was probably the result of a favorable relationship between CFV, pore size and rejected matter. As reported, [17] particles rejected by small pore size membranes could roll off under the forces generated by cross-flow, therefore, not causing membrane blockage. In the case of 500 kDa membrane, flux decline is most probably the result of particles migration through the pores, subsequent adsorption causing enhanced pore blockage or plugging.…”
Section: Membrane Characterizationsupporting
confidence: 51%
“…Prior to further chemical cleaning, the normalized flux was measured with DW to determine chemically reversible fouling. [10] The CIP procedure was determined according to the literature [17,[21][22][23][24] and some preliminary trial-and-error tests with different chemical agents, concentrations and temperatures. After the CIP process, normalized flux with DW was observed again and any remaining membrane blockage was considered as chemically irreversible fouling.…”
Section: Flux Recoverymentioning
confidence: 99%
See 1 more Smart Citation
“…Pre-treatment of spentwash with ceramic membranes prior to anaerobic digestion is reported to halve the COD from 36,000 to 18,000 mg/l (Chang et al, 1994). The total membrane area was 0.2 m 2 and the system was operated at a fluid velocity of 6.08 m/s and 0.5 bar transmembrane pressure.…”
Section: Membrane Treatmentmentioning
confidence: 99%
“…The individual use of acid gave a negative flux recovery. The cleaning cycle played an important role for the membrane regeneration and efficiency (CHANG et al 1994).…”
Section: Ceramic Membrane Regenerationmentioning
confidence: 99%