These tools will no longer be maintained as of December 31, 2024. Archived website can be found here. PubMed4Hh GitHub repository can be found here. Contact NLM Customer Service if you have questions.
260 related articles for article (PubMed ID: 27723011)
1. Experimental and CFD-PBM Study of Oxygen Mass Transfer Coefficient in Different Impeller Configurations and Operational Conditions of a Two-Phase Partitioning Bioreactor. Moradkhani H; Izadkhah MS; Anarjan N Appl Biochem Biotechnol; 2017 Feb; 181(2):710-724. PubMed ID: 27723011 [TBL] [Abstract][Full Text] [Related]
2. Oxygen mass transfer and shear stress effects on Pseudomonas putida BCRC 14365 growth to improve bioreactor design and performance. Moradkhani H; Izadkhah MS; Anarjan N; Abdi A Environ Sci Pollut Res Int; 2017 Oct; 24(28):22427-22441. PubMed ID: 28803423 [TBL] [Abstract][Full Text] [Related]
3. Using CFD simulations and statistical analysis to correlate oxygen mass transfer coefficient to both geometrical parameters and operating conditions in a stirred-tank bioreactor. Amer M; Feng Y; Ramsey JD Biotechnol Prog; 2019 May; 35(3):e2785. PubMed ID: 30758910 [TBL] [Abstract][Full Text] [Related]
4. Modeling of gas-liquid mass transfer in a stirred tank bioreactor agitated by a Rushton turbine or a new pitched blade impeller. Gelves R; Dietrich A; Takors R Bioprocess Biosyst Eng; 2014 Mar; 37(3):365-75. PubMed ID: 23828243 [TBL] [Abstract][Full Text] [Related]
5. CFD of mixing of multi-phase flow in a bioreactor using population balance model. Sarkar J; Shekhawat LK; Loomba V; Rathore AS Biotechnol Prog; 2016 May; 32(3):613-28. PubMed ID: 26850863 [TBL] [Abstract][Full Text] [Related]
6. Oxygen mass transfer in a stirred tank bioreactor using different impeller configurations for environmental purposes. Karimi A; Golbabaei F; Mehrnia MR; Neghab M; Mohammad K; Nikpey A; Pourmand MR Iranian J Environ Health Sci Eng; 2013 Jan; 10(1):6. PubMed ID: 23369581 [TBL] [Abstract][Full Text] [Related]
7. CFD evaluation of hydrophobic feedstock bench-scale fermenters for efficient high agitation volumetric mass transfer. Marx R; Liu H; Yoon S; Xie D Biotechnol J; 2024 Feb; 19(2):e2300384. PubMed ID: 38403465 [TBL] [Abstract][Full Text] [Related]
8. Characterization of the gas dispersion behavior of multiple impeller stages by flow regime analysis and CFD simulations. Bernauer S; Schöpf M; Eibl P; Witz C; Khinast J; Hardiman T Biotechnol Bioeng; 2021 Aug; 118(8):3058-3068. PubMed ID: 33990949 [TBL] [Abstract][Full Text] [Related]
9. Improvement of foam breaking and oxygen-transfer performance in a stirred-tank fermenter. Takesono S; Onodera M; Toda K; Yoshida M; Yamagiwa K; Ohkawa A Bioprocess Biosyst Eng; 2006 Mar; 28(4):235-42. PubMed ID: 16208498 [TBL] [Abstract][Full Text] [Related]
10. Validation of a CFD model for cell culture bioreactors at large scale and its application in scale-up. Xing Z; Duane G; O'Sullivan J; Chelius C; Smith L; Borys MC; Khetan A J Biotechnol; 2024 May; 387():79-88. PubMed ID: 38582408 [TBL] [Abstract][Full Text] [Related]
11. Enhancement of oxygen mass transfer in stirred bioreactors using oxygen-vectors. 1. Simulated fermentation broths. Galaction AI; Cascaval D; Oniscu C; Turnea M Bioprocess Biosyst Eng; 2004 Jul; 26(4):231-8. PubMed ID: 15042455 [TBL] [Abstract][Full Text] [Related]
12. Expressions of mass transfer coefficients of bubbles and free surface of culture tanks using the k-epsilon turbulence model. Amano K; Haga R; Murakami S J Ind Microbiol Biotechnol; 2008 Jun; 35(6):525-31. PubMed ID: 18347829 [TBL] [Abstract][Full Text] [Related]
13. Influence of a new axial impeller on K(L)a and xylanase production by Penicillium canescens 10-10c. Bakri Y; Jacques P; Shi LK; Thonart P Appl Biochem Biotechnol; 2002; 98-100():1037-48. PubMed ID: 12018228 [TBL] [Abstract][Full Text] [Related]
14. Hydrodynamic performance of a single-use aerated stirred bioreactor in animal cell culture: applications of tomography, dynamic gas disengagement (DGD), and CFD. Kazemzadeh A; Elias C; Tamer M; Ein-Mozaffari F Bioprocess Biosyst Eng; 2018 May; 41(5):679-695. PubMed ID: 29445862 [TBL] [Abstract][Full Text] [Related]
15. A novel centrifugal impeller bioreactor. II. Oxygen transfer and power consumption. Wang SJ; Zhong JJ Biotechnol Bioeng; 1996 Sep; 51(5):520-7. PubMed ID: 18629815 [TBL] [Abstract][Full Text] [Related]
16. Studies on the overall oxygen transfer rate and mixing time in pilot-scale surface aeration vessel. Kang J; Lee CH; Haam S; Koo KK; Kim WS Environ Technol; 2001 Sep; 22(9):1055-68. PubMed ID: 11816768 [TBL] [Abstract][Full Text] [Related]
17. A new dynamic model for highly efficient mass transfer in aerated bioreactors and consequences for kLa identification. Müller S; Murray DB; Machne R Biotechnol Bioeng; 2012 Dec; 109(12):2997-3006. PubMed ID: 22766628 [TBL] [Abstract][Full Text] [Related]
18. Computational-fluid-dynamics (CFD) analysis of mixing and gas-liquid mass transfer in shake flasks. Zhang H; Williams-Dalson W; Keshavarz-Moore E; Shamlou PA Biotechnol Appl Biochem; 2005 Feb; 41(Pt 1):1-8. PubMed ID: 15310285 [TBL] [Abstract][Full Text] [Related]
19. A novel impeller configuration to improve fungal physiology performance and energy conservation for cephalosporin C production. Yang Y; Xia J; Li J; Chu J; Li L; Wang Y; Zhuang Y; Zhang S J Biotechnol; 2012 Oct; 161(3):250-6. PubMed ID: 22835853 [TBL] [Abstract][Full Text] [Related]
20. A novel method of simulating oxygen mass transfer in two-phase partitioning bioreactors. Nielsen DR; Daugulis AJ; McLellan PJ Biotechnol Bioeng; 2003 Sep; 83(6):735-42. PubMed ID: 12889038 [TBL] [Abstract][Full Text] [Related] [Next] [New Search]