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Chen X, Liu Y, Jiang Y, Feng S. Radon transport carried by geogas: prediction model. ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH INTERNATIONAL 2023; 30:86656-86675. [PMID: 37436618 DOI: 10.1007/s11356-023-28616-4] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/07/2022] [Accepted: 07/01/2023] [Indexed: 07/13/2023]
Abstract
This paper provides an overview and information on radon migration in the crust. In the past several decades, numerous studies on radon migration have been published. However, there is no there is no comprehensive review of large-scale radon transport in the earth crust. A literature review was conducted to present the research on the mechanism of radon migration, geogas theory, investigation of multiphase flow, and modeling method of fractures. Molecular diffusion was long considered the primary mechanism for radon migration in the crust. However, a molecular diffusion mechanism cannot explain the understanding of anomalous radon concentrations. In contrast with early views, the process of radon migration and redistribution within the Earth may be determined by geogas (mainly CO2 and CH4). Microbubbles rising in fractured rocks may be a rapid and efficient way of radon migration, as reported by recent studies. All these hypotheses on the mechanisms of geogas migration are summarized into a theoretical framework, defined as "geogas theory." According to geogas theory, fractures are the principal channel of gas migration. The development of the discrete fracture network (DFN) method is expected to supply a new tool for fracture modeling. It is hoped that this paper will contribute to a deeper understanding of radon migration and fracture modeling.
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Affiliation(s)
- Xiaojie Chen
- School of Resource Environment and Safety Engineering, University of South China, Hengyang, 421001, Hunan, China
- Safety Technology Center, University of South China, Hengyang, 421001, Hunan, China
| | - Yong Liu
- College of Physics and Optoelectronic Engineering, Shenzhen University, Shenzhen, 518060, China
| | - Yourui Jiang
- School of Resource Environment and Safety Engineering, University of South China, Hengyang, 421001, Hunan, China
| | - Shengyang Feng
- School of Resource Environment and Safety Engineering, University of South China, Hengyang, 421001, Hunan, China.
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Aerobic oxidation of hydroxymethylfurfural using a homogeneous TEMPO/TBN catalytic system in 3D-printed milli-scale porous reactors. J Flow Chem 2023. [DOI: 10.1007/s41981-023-00264-2] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 03/08/2023]
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Zhao P, Wang H, Cheng J, Wang J, Li X, Yang C. Veiling Effects in the Measurement of Poly-disperse Particles with a Photographic Probe. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c03457] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/15/2022]
Affiliation(s)
- Peng Zhao
- School of Chemical Engineering, Sichuan University, Chengdu 610065, China
| | - Haoliang Wang
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
| | - Jingcai Cheng
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
| | - Jianfeng Wang
- School of Ecology and Environment, Zhengzhou University, Zhengzhou 450001, China
| | - Xiangyang Li
- School of Chemical Engineering, Sichuan University, Chengdu 610065, China
| | - Chao Yang
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
- School of Chemical Engineering, University of Chinese Academy of Sciences, Beijing 100049, China
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Cudak M, Rakoczy R. Hydrodynamics of gas-liquid and biophase-gas-liquid systems in stirred tanks of different scales. KOREAN J CHEM ENG 2022. [DOI: 10.1007/s11814-022-1281-2] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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Gao D, Li X, Hou B, Lu F, Ye M, Wang A, Wang X. Study of bubble behavior in high-viscosity liquid in a pseudo-2D column using high-speed imaging. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.117532] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/03/2022]
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Wu Y, Wang J, You P, Luo P. Gas phase hydrodynamics in a surface‐aerated tank with a long‐short blades agitator. AIChE J 2022. [DOI: 10.1002/aic.17680] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Yongjun Wu
- School of Chemistry & Chemical Engineering Southeast University Nanjing China
| | - Jian Wang
- Beijing System Engineering Institute Beijing China
| | - Pan You
- School of Chemistry & Chemical Engineering Southeast University Nanjing China
| | - Peicheng Luo
- School of Chemistry & Chemical Engineering Southeast University Nanjing China
- Key Laboratory of Energy Regulation Materials, Chinese Academy of Sciences Shanghai China
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Gas Dispersion in Non-Newtonian Fluids with Mechanically Agitated Systems: A Review. Processes (Basel) 2022. [DOI: 10.3390/pr10020275] [Citation(s) in RCA: 7] [Impact Index Per Article: 3.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/04/2023] Open
Abstract
Gas dispersion in non-Newtonian fluids is encountered in a broad range of chemical, biochemical, and food industries. Mechanically agitated vessels are commonly employed in these processes because they promote high degree of contact between the phases. However, mixing non-Newtonian fluids is a challenging task that requires comprehensive knowledge of the mixing flow to accurately design stirred vessels. Therefore, this review presents the developments accomplished by researchers in this field. The present work describes mixing and mass transfer variables, namely volumetric mass transfer coefficient, power consumption, gas holdup, bubble diameter, and cavern size. It presents empirical correlations for the mixing variables and discusses the effects of operating and design parameters on the mixing and mass transfer process. Furthermore, this paper demonstrates the advantages of employing computational fluid dynamics tools to shed light on the hydrodynamics of this complex flow. The literature review shows that knowledge gaps remain for gas dispersion in yield stress fluids and non-Newtonian fluids with viscoelastic effects. In addition, comprehensive studies accounting for the scale-up of these mixing processes still need to be accomplished. Hence, further investigation of the flow patterns under different process and design conditions are valuable to have an appropriate insight into this complex system.
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Xiao Y, Li X, Ren S, Mao ZS, Yang C. Hydrodynamics of gas phase under typical industrial gassing rates in a gas-liquid stirred tank using intrusive image-based method. Chem Eng Sci 2020. [DOI: 10.1016/j.ces.2020.115923] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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Abstract
The mixing process in a mechanically agitated vessel is a widespread phenomenon which plays an important role among industrial processes. In that process, one of the crucial parameters, the mixing efficiency, depends on a large number of geometrical factors, as well as process parameters and complex interactions between the phases which are still not well understood. In the last decade, large progress has been made in optimisation, construction and numerical and experimental analysis of mechanically agitated vessels. In this review, the current state in this field has been presented. It shows that advanced computational fluid dynamic techniques for multiphase flow analysis with reactions and modern experimental techniques can be used with success to analyse in detail mixing features in liquid-liquid, gas-liquid, solid-liquid and in more than two-phase flows. The objective is to show the most important research recently carried out.
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Wang H, Gao Z, Wang B, Bao Y, Cai Z. Gas dispersion and solid suspension in a three-phase stirred tank with triple impellers. Chin J Chem Eng 2020. [DOI: 10.1016/j.cjche.2019.09.013] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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Fitschen J, Maly M, Rosseburg A, Wutz J, Wucherpfennig T, Schlüter M. Influence of Spacing of Multiple Impellers on Power Input in an Industrial‐Scale Aerated Stirred Tank Reactor. CHEM-ING-TECH 2019. [DOI: 10.1002/cite.201900121] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Jürgen Fitschen
- Hamburg University of TechnologyInstitute of Multiphase Flows Eißendorfer Straße 38 21073 Hamburg Germany
| | - Marc Maly
- Hamburg University of TechnologyInstitute of Multiphase Flows Eißendorfer Straße 38 21073 Hamburg Germany
| | - Annika Rosseburg
- Hamburg University of TechnologyInstitute of Multiphase Flows Eißendorfer Straße 38 21073 Hamburg Germany
| | - Johannes Wutz
- Boehringer Ingelheim Pharma GmbH & Co. KGLate Stage USP DevelopmentBioprocess Development Biologicals Birkendorfer Strasse 65 88397 Biberach an der Riss Germany
| | - Thomas Wucherpfennig
- Boehringer Ingelheim Pharma GmbH & Co. KGLate Stage USP DevelopmentBioprocess Development Biologicals Birkendorfer Strasse 65 88397 Biberach an der Riss Germany
| | - Michael Schlüter
- Hamburg University of TechnologyInstitute of Multiphase Flows Eißendorfer Straße 38 21073 Hamburg Germany
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Power consumption and gas–liquid mass transfer in a hot-sparged three-phase stirred reactor. POWDER TECHNOL 2019. [DOI: 10.1016/j.powtec.2019.05.065] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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Bombač A, Rek Z, Levec J. Void fraction distribution in a bisectional bubble column reactor. AIChE J 2019. [DOI: 10.1002/aic.16534] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Andrej Bombač
- Laboratory for Fluid Dynamics and Thermodynamics, Faculty of Mechanical Engineering; University of Ljubljana; Ljubljana, 1000 Slovenia
| | - Zlatko Rek
- Laboratory for Fluid Dynamics and Thermodynamics, Faculty of Mechanical Engineering; University of Ljubljana; Ljubljana, 1000 Slovenia
| | - Janez Levec
- Laboratory for Chemical Reaction Engineering; National Institute of Chemistry; Ljubljana, 1000 Slovenia
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Gas-liquid mass transfer studies: The influence of single- and double-impeller configurations in stirred tanks. KOREAN J CHEM ENG 2017. [DOI: 10.1007/s11814-017-0266-z] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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Silva JP, Stragevitch L, Vinhas GM, Silva JMF. Theoretical estimation of mass transfer coefficients in solution crystallization. THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING 2017. [DOI: 10.1134/s0040579517040273] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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