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da Silva Lúcio Fernandes L, de Jesus AA, de Araújo Padilha CE, de Santana Souza DF, Cellet TSP, de Sousa EMBD, de Oliveira JA. Fabrication of methyl methacrylate-based polymer particles by miniemulsion and combined miniemulsion/emulsion polymerization using an atomization apparatus. BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING 2020. [DOI: 10.1007/s43153-020-00071-5] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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2
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Yang L, Ładosz A, Jensen KF. Analysis and simulation of multiphase hydrodynamics in capillary microseparators. LAB ON A CHIP 2019; 19:706-715. [PMID: 30676606 DOI: 10.1039/c8lc01296b] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 06/09/2023]
Abstract
The capillary microseparator is an important microfluidic device for achieving the inline separation of biphasic segmented flows. While it has found wide applications in areas such as on-chip synthesis of pharmaceuticals and fine chemicals, many aspects regarding its operating ranges and hydrodynamic details remain to be elucidated. In this work, we employ OpenFOAM computational fluid dynamics (CFD) method to systematically simulate the performance of the capillary microseparator under the retention, normal operation and breakthrough regimes. The three distinct operating regimes are in accordance with experimental observations. In addition, the simulations enable quantification of the instantaneous flow rate through each micron-scale capillary microchannel and provide detailed predictions even under very low pressure differences (∼10 Pa), both of which are difficult to achieve experimentally. Furthermore, inspired by high-resolution hydrodynamics from the CFD simulations, we develop a simple analytic expression that predicts the retention threshold of the microseparator in good agreement with the simulated results and recent computations and experimental data.
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Affiliation(s)
- Lu Yang
- Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA.
| | - Agnieszka Ładosz
- Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA.
| | - Klavs F Jensen
- Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA.
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Cordero ME, Uribe S, Zárate LG, Hernandez-Servin JA, Reyes EP, Regalado-Méndez A, Natividad R. CFD Analysis of BED Textural Characteristics on TBR Behavior: Hydrodynamics and Scaling-up. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING 2017. [DOI: 10.1515/ijcre-2017-0095] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
In recent years, CFD has played an important role in the understanding and design of TBR’s. In this work, through CFD with Eulerian approach, a three-phase heterogeneous reactor model was developed, were the accuracy of Interfacial Momentum Exchange Model (IMEM) for the gas-solid interaction, the effect of a more detailed catalytic bed geometry description, and the pellet shape over TBR hydrodynamics of two fluid phases interacting with the solid phase was studied. Then, a second model was developed, where the validated hydrodynamic model was coupled with mass transport for an HDS process of light gasoil. Additionally, in order to insight into the scaling up process of a TBRs, the proposed columns behaviors were compared against literature columns using four different ways, and it was found that the best predictions were obtained when the models’ holdup were equaled to those evaluated in literature columns. Since in reliable literature deviations in pressure drop predictions of around 30% can be found, the model results show significant improvement against literature, achieving 5 times better accuracy in predicting pressure drops, and 50% improvement in holdup prediction; the coupled model reproduces the same conversion values compared with literature data, and predicts conversions with 95% accuracy
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4
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Simulations and analysis of multiphase transport and reaction in segmented flow microreactors. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2016.12.003] [Citation(s) in RCA: 67] [Impact Index Per Article: 9.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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5
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Powell JB. Application of multiphase reaction engineering and process intensification to the challenges of sustainable future energy and chemicals. Chem Eng Sci 2017. [DOI: 10.1016/j.ces.2016.09.007] [Citation(s) in RCA: 34] [Impact Index Per Article: 4.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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Poschenrieder ST, Wagner SG, Castiglione K. Efficient production of uniform nanometer-sized polymer vesicles in stirred-tank reactors. J Appl Polym Sci 2015. [DOI: 10.1002/app.43274] [Citation(s) in RCA: 22] [Impact Index Per Article: 2.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Sarah Theresa Poschenrieder
- Institute of Biochemical Engineering; Technische Universität München; Boltzmannstraße 15 Garching D-85748 Germany
| | - Sabine Gabriele Wagner
- Institute of Biochemical Engineering; Technische Universität München; Boltzmannstraße 15 Garching D-85748 Germany
| | - Kathrin Castiglione
- Institute of Biochemical Engineering; Technische Universität München; Boltzmannstraße 15 Garching D-85748 Germany
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Lee BW, Dudukovic MP. A probabilistic model for correcting the directional sensitivity of optical probe measurements. AIChE J 2015. [DOI: 10.1002/aic.14860] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
Affiliation(s)
- Boung Wook Lee
- Chemical Reaction Engineering Laboratory (CREL), Energy, Environmental, and Chemical Engineering Dept., Washington University in St. Louis; St. Louis MO 63130
| | - Milorad P. Dudukovic
- Chemical Reaction Engineering Laboratory (CREL), Energy, Environmental, and Chemical Engineering Dept., Washington University in St. Louis; St. Louis MO 63130
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Youssef AA, Hamed ME, Al-Dahhan MH, Duduković MP. A new approach for scale-up of bubble column reactors. Chem Eng Res Des 2014. [DOI: 10.1016/j.cherd.2013.12.011] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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9
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de Mesquita CH, de Sousa Carvalho DV, Kirita R, Vasquez PAS, Hamada MM. Gas–liquid distribution in a bubble column using industrial gamma-ray computed tomography. Radiat Phys Chem Oxf Engl 1993 2014. [DOI: 10.1016/j.radphyschem.2013.02.028] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/27/2022]
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10
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An alternative method for tracking a radioactive particle inside a fluid. Appl Radiat Isot 2014; 85:139-46. [PMID: 24441678 DOI: 10.1016/j.apradiso.2013.12.006] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/23/2011] [Revised: 08/06/2013] [Accepted: 12/06/2013] [Indexed: 11/23/2022]
Abstract
The proposed tracking method describes the trajectory of a radioactive particle moving in a fluid as a sequence of small cubic cells occupied by successive particle positions. In addition, the EM reconstruction algorithm was applied to get the image of the unique cell which had the greatest probability to contain the particle at a given time of a test. Next, this information was useful to calculate the coordinates and velocities of the particle at that time. The method was tested in laboratory using a gamma radiation detection system, the radioisotope (198)Au and a mixer. According to the results, the maximum deviation found between theoretical and experimental values of the average rotating period was less than 8% and the particle's reconstructed trajectories are representative of its real movement. Thus, a paradigm shift permitted us to begin the development of an alternative method to solve the complex problem of tracking the movement of a radioactive particle inside an opaque unit.
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Youssef AA, Al-Dahhan MH, Dudukovic MP. Bubble Columns with Internals: A Review. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING 2013. [DOI: 10.1515/ijcre-2012-0023] [Citation(s) in RCA: 36] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
Most industrial bubble column reactors require the utilization of internal structures for heat transfer and/or for controlling the flow structures and back mixing in the system. The internals denote all types of innards added to a bubble column, such as perforated plates, baffles, vibrating helical springs, mixers, and heat exchanger tubes. In commercial scale bubble columns, instrumentation probes, down-comers, and risers with heat exchangers are all considered. This review presents the state-of-knowledge of bubble columns with internals. It starts with an introduction. The second section discusses the horizontal internals, and the following section examines the studies involving vertical internals.
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Becker M, Tuinier M, Rollbusch P, Ludwig M, Franke R, Grünewald M, Schlüter M. BMBF-Projekt „Multi-Phase”︁. CHEM-ING-TECH 2013. [DOI: 10.1002/cite.201300044] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
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Hickman DA, Holbrook MT, Mistretta S, Rozeveld SJ. Successful Scale-up of an Industrial Trickle Bed Hydrogenation Using Laboratory Reactor Data. Ind Eng Chem Res 2013. [DOI: 10.1021/ie4005354] [Citation(s) in RCA: 17] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
| | | | - Samuel Mistretta
- The Dow Chemical Company, Plaquemine, Louisiana 70765, United States
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Aguayo AT, Gayubo AG, Ateka A, Gamero M, Olazar M, Bilbao J. Joint Transformation of Methanol and n-Butane into Olefins on an HZSM-5 Zeolite Catalyst in Reaction–Regeneration Cycles. Ind Eng Chem Res 2012. [DOI: 10.1021/ie301142k] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Andrés T. Aguayo
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
| | - Ana G. Gayubo
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
| | - Ainara Ateka
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
| | - Mónica Gamero
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
| | - Martin Olazar
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
| | - Javier Bilbao
- Departamento de Ingeniería Química, Universidad del País Vasco, Apartado 644, 48080
Bilbao, Spain
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Liu G, Lan JA, Cao Y, Huang Z, Cheng Z, Mi Z. New insights into transient behaviors of local liquid-holdup in periodically operated trickle-bed reactors using electrical capacitance tomography (ECT). Chem Eng Sci 2009. [DOI: 10.1016/j.ces.2009.04.008] [Citation(s) in RCA: 35] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/25/2022]
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17
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