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.


BIOMARKERS

Molecular Biopsy of Human Tumors

- a resource for Precision Medicine *

126 related articles for article (PubMed ID: 25766114)

  • 41. Mixing characteristics and startup of anaerobic downflow stationary fixed film (DSFF) reactors.
    Samson R; van den Berg LB; Kennedy KJ
    Biotechnol Bioeng; 1985 Jan; 27(1):10-9. PubMed ID: 18553571
    [TBL] [Abstract][Full Text] [Related]  

  • 42. Study of hydrodynamic behavior of a laboratory scale upflow anaerobic fixed film fixed bed reactor.
    Tembhurkar AR; Mhaisalkar VA
    J Environ Sci Eng; 2006 Apr; 48(2):75-80. PubMed ID: 17913181
    [TBL] [Abstract][Full Text] [Related]  

  • 43. Detailed modeling and process design of an advanced continuous powder mixer.
    Toson P; Siegmann E; Trogrlic M; Kureck H; Khinast J; Jajcevic D; Doshi P; Blackwood D; Bonnassieux A; Daugherity PD; Am Ende MT
    Int J Pharm; 2018 Dec; 552(1-2):288-300. PubMed ID: 30268852
    [TBL] [Abstract][Full Text] [Related]  

  • 44. Insights into large-scale cell-culture reactors: II. Gas-phase mixing and CO₂ stripping.
    Sieblist C; Hägeholz O; Aehle M; Jenzsch M; Pohlscheidt M; Lübbert A
    Biotechnol J; 2011 Dec; 6(12):1547-56. PubMed ID: 21818861
    [TBL] [Abstract][Full Text] [Related]  

  • 45. Scale-down model to simulate spatial pH variations in large-scale bioreactors.
    Amanullah A; McFarlane CM; Emery AN; Nienow AW
    Biotechnol Bioeng; 2001 Jun; 73(5):390-9. PubMed ID: 11320509
    [TBL] [Abstract][Full Text] [Related]  

  • 46. Computational-fluid-dynamics (CFD) modelling of an industrial crystallizer: application to the forced-circulation reactor.
    Essemiani K; de Traversay C; Gallot JC
    Biotechnol Appl Biochem; 2004 Dec; 40(Pt 3):235-41. PubMed ID: 15139855
    [TBL] [Abstract][Full Text] [Related]  

  • 47. Fluid flow pattern in upflow reactors for anaerobic treatment of beet sugar factory wastewater.
    Heertjes PM; Kujivenhoven LI; van der Meer RR
    Biotechnol Bioeng; 1982 Feb; 24(2):443-59. PubMed ID: 18546313
    [TBL] [Abstract][Full Text] [Related]  

  • 48. Flow dynamics within a bioreactor for tissue engineering by residence time distribution analysis combined with fluorescence and magnetic resonance imaging to investigate forced permeability and apparent diffusion coefficient in a perfusion cell culture chamber.
    Dubois J; Tremblay L; Lepage M; Vermette P
    Biotechnol Bioeng; 2011 Oct; 108(10):2488-98. PubMed ID: 21557203
    [TBL] [Abstract][Full Text] [Related]  

  • 49. Axial dispersion, holdup and slip velocity of dispersed phase in a pulsed sieve plate extraction column by radiotracer residence time distribution analysis.
    Din GU; Chughtai IR; Inayat MH; Khan IH
    Appl Radiat Isot; 2008 Dec; 66(12):1818-24. PubMed ID: 18693027
    [TBL] [Abstract][Full Text] [Related]  

  • 50. Radiotracer technology in mixing processes for industrial applications.
    Othman N; Kamarudin SK
    ScientificWorldJournal; 2014; 2014():768604. PubMed ID: 24616642
    [TBL] [Abstract][Full Text] [Related]  

  • 51. Continuous water treatment by adsorption and electrochemical regeneration.
    Mohammed FM; Roberts EP; Hill A; Campen AK; Brown NW
    Water Res; 2011 May; 45(10):3065-74. PubMed ID: 21511325
    [TBL] [Abstract][Full Text] [Related]  

  • 52. Characterisation of mixing rate due to high power ultrasound.
    Yusaf TF; Buttsworth DR
    Ultrason Sonochem; 2007 Feb; 14(2):266-74. PubMed ID: 16860586
    [TBL] [Abstract][Full Text] [Related]  

  • 53. Study on the validation of the computer fluid dynamics modeling for a continuously flowing water vessel with the industrial SPECT using a radiotracer.
    Jung SH; Kim JB; Moon JH; Park JG; Kim CH; Kim HS
    Appl Radiat Isot; 2012 Oct; 70(10):2471-7. PubMed ID: 22871455
    [TBL] [Abstract][Full Text] [Related]  

  • 54. CFD optimization of continuous stirred-tank (CSTR) reactor for biohydrogen production.
    Ding J; Wang X; Zhou XF; Ren NQ; Guo WQ
    Bioresour Technol; 2010 Sep; 101(18):7016-24. PubMed ID: 20427177
    [TBL] [Abstract][Full Text] [Related]  

  • 55. Further studies related to the scale-up of high cell density Escherichia coli fed-batch fermentations: the additional effect of a changing microenvironment when using aqueous ammonia to control pH.
    Onyeaka H; Nienow AW; Hewitt CJ
    Biotechnol Bioeng; 2003 Nov; 84(4):474-84. PubMed ID: 14574706
    [TBL] [Abstract][Full Text] [Related]  

  • 56. Effect of Thermal Buoyancy on Fluid Flow and Residence-Time Distribution in a Single-Strand Tundish.
    Sheng DY; Jönsson PG
    Materials (Basel); 2021 Apr; 14(8):. PubMed ID: 33920392
    [TBL] [Abstract][Full Text] [Related]  

  • 57. Residence time distribution (RTD) of particulate foods in a continuous flow pilot-scale ohmic heater.
    Sarang S; Heskitt B; Tulsiyan P; Sastry SK
    J Food Sci; 2009 Aug; 74(6):E322-7. PubMed ID: 19723195
    [TBL] [Abstract][Full Text] [Related]  

  • 58. Xenobiotic removal efficiencies in wastewater treatment plants: residence time distributions as a guiding principle for sampling strategies.
    Majewsky M; Gallé T; Bayerle M; Goel R; Fischer K; Vanrolleghem PA
    Water Res; 2011 Nov; 45(18):6152-62. PubMed ID: 21974873
    [TBL] [Abstract][Full Text] [Related]  

  • 59. An analysis of residence time distribution patterns in a twin screw cooking extruder.
    Altomare RE; Ghossi P
    Biotechnol Prog; 1986 Sep; 2(3):157-63. PubMed ID: 20568208
    [TBL] [Abstract][Full Text] [Related]  

  • 60. Acetylation of pea isolate in a torus microreactor.
    Legrand J; Guéguen J; Berot S; Popineau Y; Nouri L
    Biotechnol Bioeng; 1997 Feb; 53(4):409-14. PubMed ID: 18634031
    [TBL] [Abstract][Full Text] [Related]  

    [Previous]   [Next]    [New Search]
    of 7.