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Oxygen mass transfer in a high solids loading three-phase internal-loop airlift reactor

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In this article, the volumetric mass transfer coefficient was determined in a three-phase internal-loop air-lifting reactor with an enlarged degassing zone, and the effect of parameters such as the airflow rate (riser superficial gas velocities between 0.01 and 0.5 m/s), solids loading (up to 30%, v/v), solics density (1023 and 1048 kg/m 3 ) and the liquid-phase properties on kLa was studied.
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This article is published in Chemical Engineering Journal.The article was published on 2001-09-15 and is currently open access. It has received 91 citations till now. The article focuses on the topics: Mass transfer coefficient & Mass transfer.

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Citations
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Journal ArticleDOI

Biomass effects on oxygen transfer in membrane bioreactors.

TL;DR: In this paper, the relative impacts of various bulk biomass characteristics on oxygen transfer were investigated in both municipal and industrial pilot and full scale submerged membrane bioreactors (MBRs) with mixed liquor suspended solids concentrations.
Journal ArticleDOI

Airlift Bioreactors: Review of Recent Advances

TL;DR: Airlift reactors are popular in the modern bioprocess research and development, over a broad spectrum of processes, which range from the production of very expensive biochemicals to wastewater treatment.
Journal ArticleDOI

Biomass Characteristics, Aeration and Oxygen Transfer in Membrane Bioreactors: Their Interrelations Explained by a Review of Aerobic Biological Processes

TL;DR: This review discusses the interrelations of the biomass characteristics (solids concentration, particle size and viscosity), the aeration intensity and the oxygen transfer in MBRs.
Journal ArticleDOI

Oxygen transfer in a gas–liquid system containing solids of varying oxygen affinity

TL;DR: In this paper, an air sparged, mechanically agitated bioreactor containing spherical solids was studied in order to determine the effect of the solid phase on oxygen mass transfer, and it was found that both nylon 6,6 and glass beads cause an enhancement of the volumetric mass transfer coefficient of up to 268%, whereas particles of silicone rubber and styrene-butadiene copolymer reduce the volume transfer coefficient by up to 63%, relative to a system without a solid phase.
References
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Book

Basic Bioreactor Design

TL;DR: Based on a graduate course in biochemical engineering, provides the basic knowledge needed for the efficient design of bioreactors and the relevant principles and data for practical process engineering with an emphasis on enzyme reactors and aerated reactors for microorganisms.
Journal ArticleDOI

Mixing and mass transfer in tall bubble columns

TL;DR: In this article, the authors measured the concentration profiles of oxygen in the liquid phase and obtained the kLa data of the various liquid phases which only depend on the gas velocity, adjusting the experimental profiles with the predictions of the axial dispersed plug flow model.
Journal ArticleDOI

Air-lift reactors in chemical and biological technology

TL;DR: In this paper, a review of air-lifted ReReF is presented, focusing on specific aspects of the air-lift ReF emphasizing their function and relevance to particular applications.
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Frequently Asked Questions (17)
Q1. What contributions have the authors mentioned in the paper "Oxygen mass transfer in a high solids loading three-phase internal-loop airlift reactor" ?

The effect of parameters such as the airflow rate ( riser superficial gas velocities between 0. 01 and 0. 5 m/s ), solids loading ( up to 30 %, v/v ), solids density ( 1023 and 1048 kg/m3 ) and the liquid-phase properties on kLa was studied. 

In aerobic bioreactors, the critical limiting factor in providing the optimal environment is the oxygen mass transfer, as a consequence of the low solubility of oxygen in fermentation media. 

Independently of the liquid-phase and the solids density, kLa diminishes with the increase of solids loading, essentially for riser superficial gas velocities higher than 0.075 m/s. 

Airflow rate and the presence of ethanol were shown to enhance the volumetric mass transfer coefficient — airflow rate by primarily increasing gas holdup and ethanol by inhibiting coalescence. 

Up to 0.075 m/s, the effect of solids loading on kLa is negligible, once the amount of gas in the reactor is so small that the solids interference in the coalescence process is not significant. 

The primary purpose of a bioreactor is to provide such environmental conditions to the microorganism that it will carry out the required reaction or transformation optimally [1]. 

According to Onken and Weiland [18] and Weiland [20], the addition of compounds that reduce bubble coalescence increases the volumetric mass transfer coefficient by a factor of about 2. 

The reduction on the volumetric mass transfer coefficient is probably the result of the coalescence process, increased by the increase of the amount of solids as reported in Freitas and Teixeira [9], what leads to a decrease on the interfacial area a. 

This increase on kLa must be due to an increase in specific interfacial area, since with the addition of alcohols the mass transfer coefficient kL decreases, by yielding an additional resistance to the interfacial mass transfer [17]. 

For each experimental condition, three replicates were done and the volumetric mass transfer coefficient was the medium value of the values obtained for the two electrodes in the three replicates. 

For t tE, Eq. (1) reduces to1 − E = e −tkLa1 − tEkLa (3)According to Van’t Riet [12], the electrode response time would have to be much smaller than the mass transfer response time of the system, 1/kLa, to be neglected. 

Observing values of mass transfer coefficient for both solids density, it can be seen that a small increase on solids density leads to a significant reduction on kLa (Fig. 2), specially for high riser superficial gas velocities. 

the volumetric mass transfer coefficient (kLa), which is normally used to characterize the mass transfer performance, plays an important role in the performance of bioreactors [1–3]. 

For riser superficial gas velocities up to 0.075 m/s, the increase is very small, while for higher airflow rates, values of kLa for aqueous ethanol solution are 1.5–2 times the values obtained with water. 

This is in agreement with the results previously obtained by the authors [10], where it was observed that the decrease of riser and downcomer gas holdup with solids density is also more pronounced for the ethanol solution, being this reflected in the results of volumetric mass transfer coefficient. 

A significant decrease on kLa resulting from a small increase of solids density (from 1023 to 1048 kg/m3) was observed, as a consequence of the effect of solids density on solids distribution in the reactor. 

The volumetric mass transfer coefficient kLa was determined by the dynamic method described by Chisti [1] and Benyhaia et al. [3].