194 related articles for article (PubMed ID: 17909861)
1. Modeling for the optimal biodegradation of toxic wastewater in a discontinuous reactor.
Betancur MJ; Moreno-Andrade I; Moreno JA; Buitrón G; Dochain D
Bioprocess Biosyst Eng; 2008 Jun; 31(4):307-13. PubMed ID: 17909861
[TBL] [Abstract][Full Text] [Related]
2. An aerobic sequencing batch reactor for 2,4,6-trinitrophenol (picric acid) biodegradation.
Weidhaas JL; Schroeder ED; Chang DP
Biotechnol Bioeng; 2007 Aug; 97(6):1408-14. PubMed ID: 17286267
[TBL] [Abstract][Full Text] [Related]
3. Enrichment of a K-strategist microbial population able to biodegrade p-nitrophenol in a sequencing batch reactor.
Martín-Hernández M; Carrera J; Pérez J; Suárez-Ojeda ME
Water Res; 2009 Aug; 43(15):3871-83. PubMed ID: 19560183
[TBL] [Abstract][Full Text] [Related]
4. Modeling the partial nitrification in sequencing batch reactor for biomass adapted to high ammonia concentrations.
Pambrun V; Paul E; Spérandio M
Biotechnol Bioeng; 2006 Sep; 95(1):120-31. PubMed ID: 16715534
[TBL] [Abstract][Full Text] [Related]
5. Effect of COD/N ratio and salinity on the performance of sequencing batch reactors.
Rene ER; Kim SJ; Park HS
Bioresour Technol; 2008 Mar; 99(4):839-46. PubMed ID: 17383178
[TBL] [Abstract][Full Text] [Related]
6. Biological waste gas treatment with a modified rotating biological contactor. II. Effect of operating parameters on process performance and mathematical modeling.
Vinage I; von Rohr PR
Bioprocess Biosyst Eng; 2003 Nov; 26(1):75-82. PubMed ID: 14505166
[TBL] [Abstract][Full Text] [Related]
7. A unified theory for upscaling aerobic granular sludge sequencing batch reactors.
Liu Y; Wang ZW; Tay JH
Biotechnol Adv; 2005 Jul; 23(5):335-44. PubMed ID: 15922130
[TBL] [Abstract][Full Text] [Related]
8. Evaluation of two control strategies for a sequencing batch reactor degrading high concentration peaks of 4-chlorophenol.
Buitrón G; Schoeb ME; Moreno-Andrade I; Moreno JA
Water Res; 2005 Mar; 39(6):1015-24. PubMed ID: 15766956
[TBL] [Abstract][Full Text] [Related]
9. Kinetic and inhibition studies for the aerobic cometabolism of 1,1,1-trichloroethane, 1,1-dichloroethylene, and 1,1-dichloroethane by a butane-grown mixed culture.
Kim Y; Arp DJ; Semprini L
Biotechnol Bioeng; 2002 Dec; 80(5):498-508. PubMed ID: 12355460
[TBL] [Abstract][Full Text] [Related]
10. Microbial adaptation to biodegradation of tert-butyl alcohol in a sequencing batch reactor.
Zhuang WQ; Tay JH; Yi S; Tay ST
J Biotechnol; 2005 Jul; 118(1):45-53. PubMed ID: 15899532
[TBL] [Abstract][Full Text] [Related]
11. 2,4-Dichlorophenol (DCP) containing wastewater treatment using a hybrid-loop bioreactor.
Dilaver M; Kargi F
Bioresour Technol; 2009 Feb; 100(3):1459-62. PubMed ID: 18778931
[TBL] [Abstract][Full Text] [Related]
12. Modeling and biokinetics in anaerobic acidogenesis of starch-processing wastewater to acetic acid.
Ahn JH; Lee S; Hwang S
Biotechnol Prog; 2004; 20(2):636-8. PubMed ID: 15059013
[TBL] [Abstract][Full Text] [Related]
13. Effect of feeding time on the performance of a sequencing batch reactor treating a mixture of 4-CP and 2,4-DCP.
Sahinkaya E; Dilek FB
J Environ Manage; 2007 Jun; 83(4):427-36. PubMed ID: 16842902
[TBL] [Abstract][Full Text] [Related]
14. Performance of an optimally filled discontinuous bioreactor degrading 4-chlorophenol.
Moreno-Andrade I; Buitrón G
Water Sci Technol; 2008; 57(12):1991-7. PubMed ID: 18587189
[TBL] [Abstract][Full Text] [Related]
15. Influence of microbial growth kinetics on steady state multiplicity and stability of a two-step nitrification (SHARON) model.
Volcke EI; Sbarciog M; Loccufier M; Vanrolleghem PA; Noldus EJ
Biotechnol Bioeng; 2007 Nov; 98(4):882-93. PubMed ID: 17461421
[TBL] [Abstract][Full Text] [Related]
16. Optimising operation of a biological wastewater treatment application.
Murphy RB; Young BR; Kecman V
ISA Trans; 2009 Jan; 48(1):93-7. PubMed ID: 18762295
[TBL] [Abstract][Full Text] [Related]
17. Practical automatic control of a sequencing batch reactor for toxic wastewater treatment.
Pat AM; Vargas A; Buitrón G
Water Sci Technol; 2011; 63(4):782-8. PubMed ID: 21330728
[TBL] [Abstract][Full Text] [Related]
18. Event-driven time-optimal control for a class of discontinuous bioreactors.
Moreno JA; Betancur MJ; Buitrón G; Moreno-Andrade I
Biotechnol Bioeng; 2006 Jul; 94(4):803-14. PubMed ID: 16523521
[TBL] [Abstract][Full Text] [Related]
19. Modeling of the Contact-Adsorption-Regeneration (CAR) activated sludge process.
Liu SG; Ni BJ; Li WW; Sheng GP; Tang Y; Yu HQ
Bioresour Technol; 2011 Feb; 102(3):2199-205. PubMed ID: 20980144
[TBL] [Abstract][Full Text] [Related]
20. Determination of kinetic parameters in the biosorption of Cr (VI) on immobilized Bacillus cereus M(1)(16) in a continuous packed bed column reactor.
Maiti SK; Bera D; Chattopadhyay P; Ray L
Appl Biochem Biotechnol; 2009 Nov; 159(2):488-504. PubMed ID: 19333567
[TBL] [Abstract][Full Text] [Related]
[Next] [New Search]
