Literature DB >> 18592489

Oxygen and carbon dioxide mass transfer and the aerobic, autotrophic cultivation of moderate and extreme thermophiles: a case study related to the microbial desulfurization of coal.

F C Boogerd1, P Bos, J G Kuenen, J J Heijnen, R G van der Lans.   

Abstract

Mass transfers of O(2), CO(2), and water vapor are among the key processes in the aerobic, autotrophic cultivation of moderate and extreme thermophiles. The dynamics and kinetics of these processes are, in addition to the obvious microbial kinetics, of crucial importance for the industrial desulfurization of high-pyritic coal by such thermophiles. To evaluate the role of the temperature on the gas mass transfer, k(L)a measurements have been used to supplement the existing published data. Oxygen mass transfer from gas (air) to liquid (5 mM H(2)SO(4) in water) phase as a function of the temperature has been studied in a laboratory-scale fermentor. At 15, 30, 45, and 70 degrees C, (k(L)a)(o) values (for oxygen) were determined under three different energy input conditions by the dynamic gassing in/out method. The (k(L)a)(o) was shown to increase under these conditions with increasing temperature, and straight lines were obtained when the logarithm of (k(L)a)(o) was plotted against the temperature. By multiplying the equilibrium concentration of O(2) in water with (k(L)a)(o) maximal, O(2) transfer capacities were calculated. It appeared that in finite of a decreased solubility of O(2) at elevated temperature in mechanically mixed fermentors the calculated transfer capacities showed only minor changes for the range between 15 and 70 degrees C. However, in an air-mixed fermentor the transfer capacity of O(2) decreased slowly but steadily.Carbon dioxide mass transfer was predicted by calculations on the basis of the data for oxygen transfer. The maximal CO(2) transfer capacity, calculated as the product of the equilibrium CO(2) concentration times (k(L)a)(c), decreased slowly as the temperature increased over the range 15-70 degrees C under all three energy input conditions. Subsequent process design calculations showed that for aerobic, autotrophic cultures, CO(2) limitation is more likely to occur than O(2) limitation.

Entities:  

Year:  1990        PMID: 18592489     DOI: 10.1002/bit.260351106

Source DB:  PubMed          Journal:  Biotechnol Bioeng        ISSN: 0006-3592            Impact factor:   4.530


  3 in total

1.  Technical insight on the requirements for CO2-saturated growth of microalgae in photobioreactors.

Authors:  Padmini Padmanabhan
Journal:  3 Biotech       Date:  2017-05-31       Impact factor: 2.406

2.  Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors.

Authors:  Johnny Lee
Journal:  Heliyon       Date:  2017-02-20

3.  Microbubble enhanced mass transfer efficiency of CO2 capture utilizing aqueous triethanolamine for enzymatic resorcinol carboxylation.

Authors:  Daniel Ohde; Benjamin Thomas; Simon Matthes; Shunya Tanaka; Paul Bubenheim; Koichi Terasaka; Michael Schlüter; Andreas Liese
Journal:  RSC Adv       Date:  2021-01-20       Impact factor: 3.361

  3 in total

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