Thin stillage fractionation using ultrafiltration: Resistance in series model

Bioprocess and Biosystems Engineering

Volumn 32, Issue 2, 2009, Pages 225-233

  Arora, Amit ^a   Dien, Bruce S ^b   Belyea, Ronald L ^c   Wang, Ping ^a   Singh, Vijay ^a   Tumbleson, M E ^a   Rausch, Kent D ^a  

^a UNIVERSITY OF ILLINOIS AT URBANA CHAMPAIGN   (United States)

^b NATIONAL CENTER FOR AGRICULTURAL UTILIZATION RESEARCH   (United States)

^c UNIVERSITY OF MISSOURI   (United States)

Author keywords

Flux; Fouling; Resistance; Thin stillage; Ultrafiltration

Indexed keywords

CAPITAL EXPENSES; CELLULOSE MEMBRANES; ETHANOL INDUSTRY; FLUX; FLUX DECLINES; FLUX RATES; FOULING; FUEL ETHANOL; MAXIMUM FLUX; MEMBRANE FILTRATION (MF); MEMBRANE SEPARATIONS; MODEL EQUATIONS; MODELING RESULTS; OPTIMUM CONDITIONS; PERMEATE FLUXES; RESISTANCE; RESISTANCE IN SERIES MODEL; SERIES MODEL; THIN STILLAGE; TOTAL RESISTANCE; TOTAL SOLIDS; TRANS-MEMBRANE PRESSURE (TMP);

BIOCHEMICAL ENGINEERING; CELLULOSE DERIVATIVES; DISTILLATION; ETHANOL; EVAPORATION; EVAPORATORS; MAINTENANCE; METAL RECOVERY; MICROFILTRATION; PLANT SHUTDOWNS; POROUS MATERIALS; ULTRAFILTRATION; VAPORS; WASTEWATER TREATMENT;

FILTRATION;

ALCOHOL;

ALCOHOL METABOLISM; ARTICLE; CONTROLLED STUDY; EVAPORATION; FRACTIONATION; MEMBRANE PERMEABILITY; MEMBRANE RESISTANCE; MEMBRANE TRANSPORT; MOLECULAR WEIGHT; NONHUMAN; PRIORITY JOURNAL; PROCESS MODEL; SEPARATION ANXIETY; TEMPERATURE; ULTRAFILTRATION;

ETHANOL; FERMENTATION; MEMBRANES, ARTIFICIAL; MODELS, THEORETICAL; PRESSURE; TEMPERATURE; ULTRAFILTRATION; ZEA MAYS;

BIOTECHNOLOGY; CELLULOSE DERIVATIVES; DISTILLATION; EFFLUENT TREATMENT; ETHANOL; EVAPORATION; EVAPORATORS; FOULING; FRACTIONATION; MAINTENANCE; POROUS MATERIALS; RESISTANCE; ULTRAFILTRATION;

ZEA MAYS;

EID: 58549102699     PISSN: 16157591     EISSN: None     Source Type: Journal    
DOI: 10.1007/s00449-008-0240-6     Document Type: Article

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