Michael Sievers

Prof. Michael Sievers

orcid

Research Focus & Metrics

Academic Career Length

32Years (1995-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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3 October 2019 in ChemBioEng Reviews
Verified
Journal Article
Open access
PDF file
TMThorben Muddemann
Thorben Muddemann
DHDennis R. Haupt
Dennis R. Haupt
MSMichael Sievers
Michael Sievers
UKUlrich Kunz
Ulrich Kunz
Regarding the treatment of (waste)water, electrochemical processes have various advantages over other methods. They are robust, easy to operate and flexible in case of fluctuating wastewater streams. In addition, a relatively broad spectrum of organic and inorganic impurities can be removed. This contribution provides an overview of electrochemical reactors for water, process water, and wastewater treatment, which are already in technical‐scale operation or subject of research. Some essential basics of electrochemical processes for the treatment of water are presented and examples for applications are given. This is followed by a description of the reactors.

1 May 2002 in Ultrasonics
Verified
Journal Article
Closed access
TOT.I. Onyeche
T.I. Onyeche
OSO. Schläfer
O. Schläfer
HBH. Bormann
H. Bormann
CSC. Schröder
C. Schröder
MSMichael Sievers
Michael Sievers

1 March 2000 in Ultrasonics
Verified
Journal Article
Closed access
OSO. Schläfer
O. Schläfer
MSMichael Sievers
Michael Sievers
HKH. Klotzbücher
H. Klotzbücher
TOT.I. Onyeche
T.I. Onyeche

1 May 2002 in Ultrasonics
Verified
Journal Article
Closed access
OSO. Schläfer
O. Schläfer
TOT. Onyeche
T. Onyeche
HBH. Bormann
H. Bormann
CSC. Schröder
C. Schröder
MSMichael Sievers
Michael Sievers

1 January 2011
Verified
Book Chapter
Closed access
MSMichael Sievers
Michael Sievers

1 February 2004 in Water Science & Technology
Verified
Journal Article
Closed access
PDF file
MSMichael Sievers
Michael Sievers
ARA. Ried
A. Ried
RKR. Koll
R. Koll
Ozonation of industrial and sewage sludge is a suitable process for minimizing the sludge production of activated sludge processes. The ozonation has the advantage for complete oxidation of volatile suspended solids (VSS) of combining partial sludge oxidation with subsequent biological oxidation. This paper describes the evaluation of two full-scale sewage sludge ozonation investigations for subsequent aerobic stabilisation as well as for subsequent anaerobic stabilisation compared to different sludge treatment processes. For both the anaerobic and aerobic application, sludge liquefying by release of 110 and 160 mg COD per g total suspended solids (TSS) has been reached at specific ozone consumption of 0.03 and 0.06 kg O3 per kg TSS, respectively. The subsequent biological treatment has reached a mass reduction of 20-35% for the aerobic and 19% for the anaerobic stabilisation. For both applications the specific ozone consumption was about 0.05 kg O3 per kg TSS to be treated. A comparison with mechanical and thermo-chemical sludge mass reduction methods shows that the mass reduction potential of ozonation is presently higher. Even though costs for sludge ozonation are higher compared to other methods, the optimisation potential for cost reduction of sludge ozonation is obvious from the results presented in this paper.