The influence of carrier size and shape in the moving bed biofilm process

Water Science and Technology

Volumn 41, Issue 4-5, 2000, Pages 383-391

  Odegaard H ^a   Gisvold, B ^b   Strickland, J ^c  

^a NORWEGIAN UNIVERSITY OF SCIENCE AND TECHNOLOGY   (Norway)

^b SINTEF   (Norway)

^c ANGLIAN WATER   (United Kingdom)

Author keywords

Kinetics; Moving bed biofilm reactor; Organic loading; Performance

Indexed keywords

ACTIVATED SLUDGE PROCESS; BIOLOGICAL FILTER BEDS; BIOMASS; CHEMICAL OXYGEN DEMAND; HIGH DENSITY POLYETHYLENES; ORGANIC COMPOUNDS; PARTICLE SIZE ANALYSIS; PERFORMANCE; REACTION KINETICS; WATER TREATMENT PLANTS;

CARRIER ELEMENTS; CARRIER SIZE; MOVING BED BIOFILM REACTORS; ORGANIC LOADING;

WASTEWATER TREATMENT;

ACTIVATED SLUDGE; BIOFILM; BIOMASS; CONFERENCE PAPER; WASTE WATER; WASTE WATER MANAGEMENT; WASTE WATER TREATMENT PLANT; WATER ANALYSIS;

GADUS MORHUA;

EID: 0033914980     PISSN: 02731223     EISSN: None     Source Type: Journal    
DOI: 10.2166/wst.2000.0470     Document Type: Conference Paper

References (2)

1. Ødegaard, H., Rusten, B. and Westrum, T. (1994). A new moving bed biofilm reactor - Applications and results. Wat.Sci.Tech. 29(10-11), 157-165.
2. Ødegaard, H., Rusten, B. and Siljudalen, J. (1998). The development of the moving bed biofilm process -from idea to commercial product. European Water Management 2(2).