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Journal articles on the topic 'CLORIDE PACKED BED SYSTEMS'

Author: Grafiati

Published: 11 September 2023

Last updated: 31 July 2025

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1

Sanderson, T. M., and G. T. Cunningham. "Packed bed thermal storage systems." Applied Energy 51, no. 1 (1995): 51–67. http://dx.doi.org/10.1016/0306-2619(94)00045-g.

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2

McQuade, D., A. Bogdan, B. Mason, and K. Sylvester. "Flow Systems with a Packed-Bed Microreactor." Synfacts 2007, no. 5 (2007): 0551. http://dx.doi.org/10.1055/s-2007-968489.

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3

Bendre, Aayush, Hardik Birla, Chetan Choudhary, Gayatri Potbhare, Burhanuddin Jawadwala, and Satish Inamdar. "Water from Air: Desiccant System Design and Simulation." International Journal of Research in Advent Technology 9, no. 4 (2021): 1–7. http://dx.doi.org/10.32622/ijrat.94202101.

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Air water generators that harvest water from air humidity have the potential to counter the ever-rising problem of drinking water scarcity. There are many different types of air water generation systems that work on various different principles. Desiccant based air water generation systems work on the principle of moisture absorption, consisting of a packed bed dehumidifier that absorbs the moisture from air. This reduces the energy requirement of the system. To discuss the efficiency of the system, it is crucial to understand the working of the packed bed column. In this paper, a mathematical

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4

Kim, Dong-Seon. "Performance Characteristics of Packed-bed Thermal Storage Systems." Korean Journal of Air-Conditioning and Refrigeration Engineering 34, no. 4 (2022): 172–82. http://dx.doi.org/10.6110/kjacr.2022.34.4.172.

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5

Foumeny, E. A., A. Kulkarni, S. Roshani, and A. Vatani. "Elucidation of pressure drop in packed-bed systems." Applied Thermal Engineering 16, no. 3 (1996): 195–202. http://dx.doi.org/10.1016/1359-4311(95)00002-x.

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6

Akanji, Olaitan L., and Andrei V. Kolesnikov. "Modeling of heat and mass transfer in LaNi5 matrix during hydrogen absorption-desorption cycle." Polish Journal of Chemical Technology 14, no. 3 (2012): 71–76. http://dx.doi.org/10.2478/v10026-012-0087-0.

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Packed bed reactors using metal hydride are attracting a lot of attention as potential hydrogen storage systems. Some operational and design variables are major constraints to obtain a proper infl ow/outfl ow of hydrogen into a metal hydride reactor. These variables include packed bed thermal conductivity, porosity, pressure and temperature distributions in the reactor during the absorption/desorption cycle. They also cause a mechanical stress induced by temperature gradient. In this paper, two dimensional models are implemented in COMSOL multiphysics to simulate the hydrogen fl ow, pressure a

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7

El ouali, Abdelmajid, Hajar Zennouhi, Wafaa Benomar, Najma Laaroussi, Tarik El rhafik, and Tarik Kousksou. "Energetic Analysis of Packed Bed Latent Heat Storage Systems." ITM Web of Conferences 46 (2022): 01001. http://dx.doi.org/10.1051/itmconf/20224601001.

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Nowadays, with the rapid growths in world population and economy, the world energy demand and consumption have increased enormously which led to a wide variety of harsh environmental impacts [1]. As a potential solution for energy conservation storing the excess energy to fill the gap between energy supply and demand, using phase change materials (PCMs) has received much attention. Thermal energy storage with PCM is a promising technology based on the principle of latent heat thermal energy storage (LHTES)[2], where PCM absorbs or releases large amounts of energy at a certain temperature durin

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8

Elouali, A., T. Kousksou, T. El Rhafiki, et al. "Physical models for packed bed: Sensible heat storage systems." Journal of Energy Storage 23 (June 2019): 69–78. http://dx.doi.org/10.1016/j.est.2019.03.004.

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9

Oró, Eduard, Albert Castell, Justin Chiu, Viktoria Martin, and Luisa F. Cabeza. "Stratification analysis in packed bed thermal energy storage systems." Applied Energy 109 (September 2013): 476–87. http://dx.doi.org/10.1016/j.apenergy.2012.12.082.

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10

BENYAHIA, FARID. "On the Modeling of Flow in Packed Bed Systems." Particulate Science and Technology 22, no. 4 (2004): 367–78. http://dx.doi.org/10.1080/02726350490516028.

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11

Singh, Harmeet, R. P. Saini, and J. S. Saini. "A review on packed bed solar energy storage systems." Renewable and Sustainable Energy Reviews 14, no. 3 (2010): 1059–69. http://dx.doi.org/10.1016/j.rser.2009.10.022.

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12

Georgousis, Nikolaos, Jan Diriken, Michel Speetjens, and Camilo Rindt. "Comprehensive review on packed-bed sensible heat storage systems." Journal of Energy Storage 121 (June 2025): 116516. https://doi.org/10.1016/j.est.2025.116516.

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13

Souza, G. F. M. V., R. Béttega, R. F. Miranda, O. S. H. Mendoza, and M. A. S. Barrozo. "Experimental Analysis of Heat Transfer inside Packed Beds of Soybean Seeds." Materials Science Forum 727-728 (August 2012): 1818–23. http://dx.doi.org/10.4028/www.scientific.net/msf.727-728.1818.

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Several applications in chemical industry use randomly packed bed of particles, such as particulate separation systems, chemical reactors or fixed bed drying. Fluid dynamic behavior, heat and mass transfer, in addition to structural properties of the bed are fundamental issues to design of these processes. Several studies about heat transfer in packed beds aiming drying application have been performed in order to contribute with the process. Seeds drying temperature is especially important for the seeds quality indices and must be carefully controlled in drying process. In this paper temperatu

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14

Koçak, Burcu, and Halime Paksoy. "Packed-bed sensible thermal energy storage system using demolition wastes for concentrated solar power plants." E3S Web of Conferences 113 (2019): 01014. http://dx.doi.org/10.1051/e3sconf/201911301014.

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This paper presents a study on development of a packed-bed storage system for CSP applications. In this system, demolition wastes from urban regeneration projects in Turkey has been investigated as potential STESM for cost effective storage systems. Schumann’s two-phase one-dimensional model was used to evaluate the optimal design parameters. Effect of operational and geometrical design parameters such as mass velocity, porosity, aspect ratio of packed bed, packing diameter were assessed on storage performance. The system showed the best performance with low bed void fraction, low mass flow ra

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15

Rabi’, Ayah Marwan, Jovana Radulovic, and James M. Buick. "Comparative Study of Different Gases for Packed-Bed Thermal Energy Storage Systems." Energies 18, no. 5 (2025): 1307. https://doi.org/10.3390/en18051307.

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In recent years, packed-bed systems for large-scale applications have emerged as a highly promising design for Thermal Energy Storage systems because of their high thermal efficiency and economic feasibility. Large-scale application systems typically include packed-bed thermal energy stores as essential components, enabling effective integration with renewable energy and processed heat. The packed-bed systems investigated in this paper utilise Magnesia as the storage medium and optimised parameters, which have previously been identified through research involving charging and discharging cycle

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16

Rabi’, Ayah Marwan, Jovana Radulovic, and James M. Buick. "Packed Bed Thermal Energy Storage System: Parametric Study." Thermo 4, no. 3 (2024): 295–314. http://dx.doi.org/10.3390/thermo4030016.

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The use of thermal energy storage (TES) contributes to the ongoing process of integrating various types of energy resources in order to achieve cleaner, more flexible, and more sustainable energy use. Numerical modelling of hot storage packed bed storage systems has been conducted in this paper in order to investigate the optimum design of the hot storage system. In this paper, the effect of varying design parameters, including the diameter of the packed bed, the storage material, the void fraction, and the aspect ratio of the packed bed, on storage performance was investigated. COMSOL Multiph

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17

Li, Haijing, and Federico Toschi. "Plasma-induced catalysis: towards a numerical approach." Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences 378, no. 2175 (2020): 20190396. http://dx.doi.org/10.1098/rsta.2019.0396.

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A lattice Boltzmann (LB) model is developed, validated and used to study simplified plasma/flow problems in complex geometries. This approach solves a combined set of equations, namely the Navier–Stokes equations for the momentum field, the advection–diffusion and the Nernst–Planck equations for electrokinetic and the Poisson equation for the electric field. This model allows us to study the dynamical interaction of the fluid/plasma density, velocity, concentration and electric field. In this work, we discuss several test cases for our numerical model and use it to study a simplified plasma fl

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18

Mrinal, Bhowmik, Giampieri Alessandro, Roskilly Anthony Paul, and Ma Zhiwei. "Performance assessment of packed bed systems for humidity control in greenhouse applications: An experimental-based AI modeling approach." International Journal of Agricultural Science and Food Technology 10, no. 2 (2024): 061–67. http://dx.doi.org/10.17352/2455-815x.000208.

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Optimal humidity control is essential for enhancing crop yields and ensuring favorable growth conditions in greenhouse agriculture. Packed bed systems have emerged as effective tools for regulating humidity levels, yet accurately assessing their performance remains unexplored, especially for temperate oceanic climates. This paper presents a packed-bed system with water as the working fluid to increase the humidity level during the winter for greenhouse cultivation. Accordingly, an experimental setup is developed, and a detailed parametric study is conducted. Further, an artificial intelligence

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19

Calderón-Vásquez, Ignacio, Eduardo Cortés, Jesús García, et al. "Review on modeling approaches for packed-bed thermal storage systems." Renewable and Sustainable Energy Reviews 143 (June 2021): 110902. http://dx.doi.org/10.1016/j.rser.2021.110902.

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20

Kumar, Anil, and Man-Hoe Kim. "Solar air-heating system with packed-bed energy-storage systems." Renewable and Sustainable Energy Reviews 72 (May 2017): 215–27. http://dx.doi.org/10.1016/j.rser.2017.01.050.

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21

Chung, Tsair-Wang. "Predictions of moisture removal efficiencies for packed-bed dehumidification systems." Gas Separation & Purification 8, no. 4 (1994): 265–68. http://dx.doi.org/10.1016/0950-4214(94)80007-3.

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22

Ortega‐Fernández, Iñigo, Irantzu Uriz, Asier Ortuondo, et al. "Operation strategies guideline for packed bed thermal energy storage systems." International Journal of Energy Research 43, no. 12 (2018): 6211–21. http://dx.doi.org/10.1002/er.4291.

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23

Lipiński, W., E. Guillot, G. Olalde, and A. Steinfeld. "TRANSMITTANCE ENHANCEMENT OF PACKED-BED PARTICULATE MEDIA." Experimental Heat Transfer 21, no. 1 (2008): 73–82. http://dx.doi.org/10.1080/08916150701647843.

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24

Mishra, R. S. "Thermal Performance of Low Cost Packed Bed Thermal Energy Storage Systems for Space Heating and Crop Drying Applications in the Rural Areas." International Journal of Advance Research and Innovation 1, no. 3 (2013): 95–100. http://dx.doi.org/10.51976/ijari.131313.

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Low grade thermal energy is often required in the agricultural products, the conventional fuels most commonly used are diesel, petrol, bio-diesel, CNG, LPG, electricity, wood, agro waste etc. are available very costly day by day and are getting in the rural areas. The alternative is to use the solar energy thermal storage systems based on water is air required as a basic components in the low grade thermal energy utilization. A simple thermal analysis for open and close loop packed bed collector cum storage system has been carried out to study the performance of the system using different type

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25

Bankovic-Ilic, Ivana, Marija Miladinovic, and Vlada Veljkovic. "Continuous reciprocating plate and packed bed multiphase reactors in biodiesel production: Advancements and challenges." Chemical Industry, no. 00 (2024): 10. http://dx.doi.org/10.2298/hemind230630010b.

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Biodiesel, a renewable and environmentally friendly alternative to conventional fossil fuels, has gained significant attention over the last two decades. Continuous production of biodiesel offers efficiency, productivity, and scalability advantages. This paper provides a concise overview of continuous reactor systems for biodiesel production, focusing on two specific systems-the reciprocating plate reactor and the packed bed reactor-subjects of the authors' extensive research. A thorough comparison of these reactors, spanning biodiesel yield, reaction kinetics, and conversion efficiency, under

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26

Tien, C. L. "Thermal Radiation in Packed and Fluidized Beds." Journal of Heat Transfer 110, no. 4b (1988): 1230–42. http://dx.doi.org/10.1115/1.3250623.

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The present work gives an overview of the existing knowledge on radiative transfer in packed and fluidized beds. Special emphasis is given to the proper usage and determination of radiation characteristics of the particles in these systems. Models that treat the particulate bed as a continuum are discussed along with those that consider the system as discontinuous, i.e., accounting for the phase boundaries between the gas and the particles. Existing experimental techniques for determining the radiative properties are presented, and the published bed transmittance and reflectance data are discu

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27

GENC, Alper Mete, Ziya Haktan KARADENIZ, Orhan EKREN, and Macit TOKSOY. "A Novel Spherical Packed Bed Application on Decentralized Heat Recovery Ventilation Units." E3S Web of Conferences 111 (2019): 01012. http://dx.doi.org/10.1051/e3sconf/201911101012.

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Decentralized heat recovery ventilation (HRV) systems are assumed as simple solutions to obtain a healthy and comfortable indoor environment. A wall or window mounted compact version of decentralized HRV systems (mono unit) are used for small scale, mostly residential applications. A fan and a heat exchanger are the critical components of this compact system. The flow capacity of these units are down to 10 m3/h, where efficiencies over 90% are commonly declared by the manufacturers. On the other hand, spherical packed beds (SPD) are widely used in the heat transfer applications such as; chemic

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28

Salarian, Hesamoddin. "An Analysis of Packed Bed Liquid Desiccant System." Applied Mechanics and Materials 390 (August 2013): 680–84. http://dx.doi.org/10.4028/www.scientific.net/amm.390.680.

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In this paper a new type of open absorption the liquid desiccant, air conditioning system will be introduced. The dehumidifier and regenerator play the most important role in this system.For liquid-gas contact, packed towers with low pressure drop provide good heat and mass transfer characteristics for compact designs. Thus, this analysis considers the packed tower liquid desiccant systems. The experimental data have been obtained from a built prototype of liquid desiccant system in a packed bed unit with a surface area per unit volume ratio of 125m2/m3, the liquid desiccant, viz lithium chlor

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29

Satyawali, Yamini, Lieve Cauwenberghs, Miranda Maesen, and Winnie Dejonghe. "Lipase catalyzed solvent free synthesis of monoacylglycerols in various reaction systems and coupling reaction with pervaporation for in situ water removal." Chemical Engineering & Processing 166 (May 26, 2021): 108475. https://doi.org/10.1016/j.cep.2021.108475.

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This work reports a practical comparison of simple reaction systems for enzymatic production of monoacylglycerols (MAG) from lauric- and caprylic acid. Two approaches namely shake flasks and packed bed reactor (from 60 g to 3 kg scale) were compared as well as water removal strategies such as adsorption on molecular sieves, N2 stripping and hydrophilic pervaporation, were studied. In all the reactor systems high fatty acid conversion (>90%) was achieved in solvent free conditions. The product profile obtained showed 35 wt% - 50 wt % MAG in various systems and was related to final fatty acid

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30

Yakovlev, Igor A., Sergey D. Zambalov, and Vladimir A. Skripnyak. "Numerical Simulation of Flow Distribution in the Packed Bed Reactor with the Supply Nozzle Placed on the Sidewall." Key Engineering Materials 743 (July 2017): 383–88. http://dx.doi.org/10.4028/www.scientific.net/kem.743.383.

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Flow distribution is an important process step of many technologies such as heating or cooling systems, microchannel reactors, bubble columns and fixed- or fluidized-bed reactors etc. The present work is devoted to numerical simulation of flow distribution in the pre-reactor unit of the packed bed reactor used for filtrating combustion of fuel mixtures. A special modification of the construction is considered namely the construction with a nozzle for fuel mixture supply placed on the sidewall of the apparatus. The problem formulation, the best practices and opportunities of numerical simulatio

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31

Boskovic-Vragolovic, Nevenka, Danica Brzic, and Zeljko Grbavcic. "Mass transfer between a fluid and an immersed object in liquid-solid packed and fluidized beds." Journal of the Serbian Chemical Society 70, no. 11 (2005): 1373–79. http://dx.doi.org/10.2298/jsc0511373b.

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The mass transfer coefficient between fluid and an immersed sphere in liquid packed and fluidized beds of inert spherical particles have been studied experimentally using a column 40 mm in diameter. The mass transfer data were obtained by studying the transfer of benzoic acid from the immersed sphere to flowing water using the dissolution method. In all runs, the mass transfer rates were determined in the presence of inert glass particles 0.50-2.98 mm in diameter. The influence of different parameters, such as: liquid velocity, particles size and bed void age, on the mass transfer in packed an

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32

Akdogan, Hatice Ardag. "Immobilized Coprinus plicatilis Biodegradation of Fluorene in Two Different Packed-Bed Reactors." Journal of AOAC INTERNATIONAL 98, no. 1 (2015): 124–29. http://dx.doi.org/10.5740/jaoacint.12-182.

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Abstract The biodegradation of fluorene by immobilized Coprinus plicatilis was studied in pinewood and foam glass bead-packed reactors. The reactors were operated in a sequencing batch system. Removal efficiency increased over time and elevated influent fluorene concentration (85 mg/L) was removed 100% in 24–30 h batch cycles. Increased laccaseactivity was detected with the introduction of the compounds, and optimum activity corresponded to optimum removal periods. Significantly higher laccase activity (16.7–19 U/L) was detected in the glassbead-packed reactor compared to the pinewood-packed r

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33

FAHMY, FATEN H., and ZEINAB S. ABDEL-REHIM. "Efficient Design of Desalination System Using Photovoltaic and Packed Bed Systems." Energy Sources 20, no. 7 (1998): 615–29. http://dx.doi.org/10.1080/00908319808970082.

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34

Bindra, Hitesh, Pablo Bueno, Jeffrey F. Morris, and Reuel Shinnar. "Thermal analysis and exergy evaluation of packed bed thermal storage systems." Applied Thermal Engineering 52, no. 2 (2013): 255–63. http://dx.doi.org/10.1016/j.applthermaleng.2012.12.007.

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35

Adebiyi, George A. "A Second-Law Study on Packed Bed Energy Storage Systems Utilizing Phase-Change Materials." Journal of Solar Energy Engineering 113, no. 3 (1991): 146–56. http://dx.doi.org/10.1115/1.2930486.

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Thermal modeling of packed bed, thermal energy storage systems has traditionally been limited to first-law considerations. The exceptions include a few second-law studies, noted in the Introduction, of sensible heat storage systems and the latent heat storage systems. The cited second-law studies treat the storage and removal processes essentially as “batch” heating and cooling. The approximation effectively ignores the significant temperature gradient, especially in the axial direction, in the storage medium over a substantial portion of both the storage and removal processes. The results pre

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36

Mohd Pauzi, Mohd Mu’Izzuddin, Nurulhuda Azmi, and Kok Keong Lau. "Emerging Solvent Regeneration Technologies for CO2 Capture through Offshore Natural Gas Purification Processes." Sustainability 14, no. 7 (2022): 4350. http://dx.doi.org/10.3390/su14074350.

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It is estimated that 40% of natural gas reservoirs in the world are contaminated with acid gases (such as hydrogen sulfide and carbon dioxide), which hinder exploitation activities. The demand for natural gas will increase by 30% from 2020 to 2050, with the rise of industrial activities and the lifting of travel restrictions. The long-term production of these high acid-gas fields requires mitigation plans, which include carbon capture, utilization, and a storage process to reduce carbon emissions. Absorption is one the most established technologies for CO2 capture, yet it suffers from extensiv

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37

Hartman, Miloslav, and Robert W. Coughlin. "On the Incipient Fluidized State of Solid Particles." Collection of Czechoslovak Chemical Communications 58, no. 6 (1993): 1213–41. http://dx.doi.org/10.1135/cccc19931213.

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A comprehensive study has been reported on all aspects of the transition of packed bed to the state of incipient fluidization (point of minimum fluidization, onset of fluidization): particle size and shape, size distribution in a batch of particles, fixed bed voidage, pressure drop through a packed bed and oneset of fluidization. A number of predictive equations have been compared that were proposed to estimate the minimum fluidization velocity. All the equations tested do not have any flow limitations and are applicable to laminar, transitional as well as to turbulent flow regime. While some

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38

Wojcieszak, Paweł, and Ziemowit Malecha. "Cryogenic energy storage system coupled with packed-bed cold storage." E3S Web of Conferences 44 (2018): 00190. http://dx.doi.org/10.1051/e3sconf/20184400190.

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Cryogenic Energy Storage (CES) systems are able to improve the stability of electrical grids with large shares of intermittent power plants. In CES systems, excess electrical energy can be used in the liquefaction of cryogenic fluids, which may be stored in large cryogenic vessels for long periods of time. When the demand for electricity is high, work is recovered from the cryogen during a power cycle using ambient or waste heat as an upper heat source. Most research is focused on liquid air energy storage (LAES). However, natural gas can also be a promising working fluid for the CES system. T

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39

CHEN, CHUN-YU, and CHANG-CHUEN SUN. "Non-linear inferential control of packed-bed reactors." International Journal of Systems Science 23, no. 7 (1992): 1063–82. http://dx.doi.org/10.1080/00207729208949366.

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40

Lasek, Lukasz, Anna Zylka, Jaroslaw Krzywanski, Dorian Skrobek, Karol Sztekler, and Wojciech Nowak. "Review of Fluidized Bed Technology Application for Adsorption Cooling and Desalination Systems." Energies 16, no. 21 (2023): 7311. http://dx.doi.org/10.3390/en16217311.

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Adsorption technology utilizes low-temperature renewable and waste heat sources for cost-effective and environmentally friendly cooling and water desalination systems. However, the problem with existing adsorption refrigerators is the low COP. This is caused by poor heat and mass transfer in existing packed bed designs. The solution to this problem lies in the use of fluidized bed technology, which enhances heat and mass transfer mechanisms. Various approaches to the construction and operation of adsorption systems with a fluidized bed of adsorbent can be found in the literature; hence, the ai

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41

Priest, Cameron, Yuqing Meng, Lucun Wang, and Dong Ding. "Ethylene Production from Oxidative Coupling of Methane in Solid Oxide Electrochemical Cells." ECS Meeting Abstracts MA2022-02, no. 49 (2022): 1936. http://dx.doi.org/10.1149/ma2022-02491936mtgabs.

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The oxidative coupling of methane (OCM) to ethylene is a potentially more economical and environmentally benign approach for ethylene production compared to conventional high temperature thermal cracking of natural gas. The OCM reaction is typically conducted in packed bed flow reactors under thermal conditions in the presence of a heterogeneous catalyst. However, due to the intrinsic thermodynamic and kinetic constraints, the existing catalytic systems operated in packed bed reactors have not yet met the techno-economic requirements for the commercialization of this process. As an alternative

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42

Vagliasindi, F. G. A., and Mark M. Benjamin. "Arsenic removal in fresh and nom-preloaded ion exchange packed bed adsorption reactors." Water Science and Technology 38, no. 6 (1998): 337–43. http://dx.doi.org/10.2166/wst.1998.0269.

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Arsenic speciation and removal in continuous-flow packed bed adsorption reactors was investigated using a strong base anion exchange resin as the adsorbent. Preloading of the media was investigated passing arsenic-free Lake Washington water through columns packed with the resin prior to feeding influent spiked with arsenic. NOM preloading did not affect the systems, but sulfate adsorbed during the preloading and the subsequent adsorption steps caused chromatographic displacement of the adsorbed arsenic. Significant arsenic speciation changes occurred in the arsenic-spiked feeding solution that

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43

Kobayashi, Kwihwan, Teruhiko Tanaka, Yoshihiro Kon, Hajime Kawanami, and Nagatoshi Koumura. "Enhancing continuous-flow reactions via compression-molding of solid catalysts and dilutants in packed-bed systems." RSC Advances 14, no. 10 (2024): 6598–602. http://dx.doi.org/10.1039/d3ra08088a.

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In this study, we present an improved packed-bed system designed for continuous-flow reactions using platinum (Pt)-black powder and silica gel (SiO2). The Pt-leaching from the reaction column is suppressed via compression-molding of the Pt and SiO2.

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44

Esence, Thibaut, Arnaud Bruch, Jean-François Fourmigué, and Benoit Stutz. "A versatile one-dimensional numerical model for packed-bed heat storage systems." Renewable Energy 133 (April 2019): 190–204. http://dx.doi.org/10.1016/j.renene.2018.10.012.

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45

Mawire, Ashmore, Tlotlo M. Lefenya, Chidiebere S. Ekwomadu, Katlego A. Lentswe, and Adedamola B. Shobo. "Performance comparison of medium temperature domestic packed bed latent heat storage systems." Renewable Energy 146 (February 2020): 1897–906. http://dx.doi.org/10.1016/j.renene.2019.08.063.

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46

Sanderson, T. M., and G. T. Cunningham. "Performance and efficient design of packed bed thermal storage systems. Part 1." Applied Energy 50, no. 2 (1995): 119–32. http://dx.doi.org/10.1016/0306-2619(95)92628-7.

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47

Rejish Kumar, V. J., Cini Achuthan, N. J. Manju, Rosamma Philip, and I. S. Bright Singh. "Activated packed bed bioreactor for rapid nitrification in brackish water hatchery systems." Journal of Industrial Microbiology & Biotechnology 36, no. 3 (2008): 355–65. http://dx.doi.org/10.1007/s10295-008-0504-9.

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48

Mohammed, Ramy H., Osama Mesalhy, Mohamed L. Elsayed, and Louis C. Chow. "Performance evaluation of a new modular packed bed for adsorption cooling systems." Applied Thermal Engineering 136 (May 2018): 293–300. http://dx.doi.org/10.1016/j.applthermaleng.2018.02.103.

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Knödler, Philipp. "Thermo-Mechanical Investigations of Packed Beds for High Temperature Heat Storage: Continuum Modeling." Applied Sciences 9, no. 12 (2019): 2569. http://dx.doi.org/10.3390/app9122569.

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Abstract:

Thermal energy storage (TES) systems are central elements for various types of new power plant concepts, whereat packed beds represent a promising storage inventory option. Due to thermal expansion and shrinking of the packed bed’s particles during cyclic thermal charging and discharging operation, high technical risks arise, and possibly lead to material failure. In order to accurately design the heat storage system, suitable tools for calculating induced forces and stresses are mandatory. Continuum models offer time efficient simulation results, but are in need of effective packed bed parame

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Hui, Ji, Nie Song-Lin, and Bai Xiao-Rong. "Simulation on mechanism of contamination mitigation through Higee and hydrocyclone techniques in fluid power system." Proceedings of the Institution of Mechanical Engineers, Part E: Journal of Process Mechanical Engineering 232, no. 1 (2016): 77–93. http://dx.doi.org/10.1177/0954408916684161.

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Abstract:

In this study, an innovative Higee hydraulic oil purification device capable of removing the solid particle contaminants and water moisture simultaneously is developed for dealing with the contamination control problem of fluid power systems. The purification device is considered as a combination of two units (hydrocyclone separator and rotating packed bed) according to different separation functions. The mathematical models about the migration regularity and dynamic behavior of different phases have been established, in which discrete phase model model is employed to simulate the solid partic

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