The relevance application of dye cannot be overemphasized in our vicinity today, ranging from paintings, textiles, artistic purposes. Also, several other industrial applications including the cosmetics, leather, paper and even food industry. Notwithstanding its wide application, research has shown that the production of waste water containing synthetic dyes are deleterious to the environment and the ecosystem and therefore needs to be removed for the safety of the ecosystem. Several techniques like reverse osmosis, membrane filtration and coagulation can be used for removal of dyes. Some of these methods, despite their efficiency in wastewater treatment, they are expensive and sometimes complex to set up, therefore there is need for cheaper, affordable and simple method of wastewater treatment. Adsorption, mostly with waste biomass has proven to be a good and inexpensive method of dye removal from waste water. Therefore, this article reviewed adsorption of methylene blue dye unto sandbox seed biosorbent in a fixed bed continuous adsorption column. This review shows that there is still more to be done in terms of combining two or more different approaches in predicting and modelling adsorption of methylene blue removal from effluent water in order to obtain optimum result from treated water.
Published in | Journal of Energy, Environmental & Chemical Engineering (Volume 10, Issue 2) |
DOI | 10.11648/j.jeece.20251002.12 |
Page(s) | 56-67 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2025. Published by Science Publishing Group |
Adsorption, Computational Fluid Dynamics, Artificial Neural Network, Dye
Column adsorption model | Model equation |
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Thomas model (TM) |
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Bed depth service time model (BDST) |
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Adam and Bohart model (ABM) |
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Yoon–Nelson model (YNM) |
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Clark model (CM) |
|
Wolborska model (WM) |
|
Modifed dose response model (MDRM) |
|
Wang model |
|
S/n | Work done | Adsorbent/adsorbate | Findings | Modeling/optimization tool | Method of adsorption | author |
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1 | Application of RSM for Methylene Blue dye removal from aqueous solution using low-cost adsorbent | Charred parthenium/methylene blue dye | 93.4% removal of methylene blue was obtained at 25 mg/L initial concentration, 0.2 g of CP, pH of 7 and temperature of 35°C. also found out that pH has the greatest influence on dye recovery from spent adsorbent | RSM | Batch adsorption | [33] |
3 | Application of RSM for Bioremoval of Methylene Blue Dye from Industrial Wastewater onto Sustainable Walnut Shell (Juglans regia) Biomass | Walnut shell biomass/methylene blue dye | Maximum Methylene blue die removal of (97.70%) was obtained with a 30 mg/L, 1.5 gm of biomass, pH of 6, and for 60 min at 25°C. | RSM | Batch adsorption | [8] |
4 | Modeling of adsorption of Methylene Blue dye on Ho-CaWO4 nanoparticles using RSM and ANN techniques | Ho-CaWO4 nanoparticles/methylene blue dye | the RSM model was more acceptable since it has the lowest RMSE and AAD compared to the ANN model. Optimum MB removal of 71.17% was obtained at pH of 2.03, contact time of 15.16 min, Ho-CaWO4 nanoparticles dose of 1.91 g/L, and MB concentration of 100.65 mg/L. Maximum adsorption capacity (qm) of 103.09 mg/g was obtained. | ANN and RSM | Batch adsorption | [52] |
5 | ANN modeling of adsorption of methylene blue by NaOH-modified rice husk in a fixed-bed column system | Rice husk/methylene blue | Results show that with increasing bed height and decreasing flow rate, the breakthrough time was delayed. the ANN model is the most suitable model to describe the fixed bed adsorption of MB by modified rice husk | ANN | Fixed bed column adsorption system | [9] |
6 | Investigation of an Adsorptive Indigo Carmine Dye Removal via Packed Bed Column: Experiments and Computational Fluid Dynamics Simulation | graphene nanoadsorbent/Indigo Carmine Dye | Their result shows that High bed depth, low flow rate and high initial dye concentration increased the adsorption capacity of the adsorbent. Also, the optimum removal efficiency of the adsorbate was achieved to be 67% at flow rate, bed depth, and concentration of 1 ml/min, 28 cm and 10 ppm, respectively | CFD | Packed bed column and batch adsorption system | [53] |
7 | Adsorptive removal of methylene blue dye from aqueous streams using photocatalytic CuBTC/ZnO chitosan composites | CuBTC/ZnO chitosan composite/ Methylene blue dye | Their result shows that the pseudo second order and Langmuir models were the best fit for the adsorption process, at adsorbent dosage of 1.6 g/L, and 90 min a removal efficiency of 98.75% was achieved | Batch process | [54] | |
8 | Prediction of methyl orange dye (MO) adsorption using activated carbon with an artificial neural network optimization modeling | Date seed activated carbon/Methylene blue dye | The system was found to follow the pseudo second order kinetics at R2 value of 0.9973. Also, it was discovered that the Langmuir model performed better with an R2 value of0.9902 | ANN | Batch adsorption | [55] |
9 | use of RSM and ANN approach for methylene blue removal by adsorption onto water hyacinth | Water hyacinth / methylene blue | Color removal of 96.649% was obtained experimentally at the optimized condition. A comparison between the experimental data and model results shows a high R2 value (R2 RSM = 0.99 and R2 ANN = 0.98) and showed that the two models predicted MB removal indicating that WH is a good adsorbent. | ANN, RSM | Batch adsorption | [56] |
S/n | Work done | Adsorbent/adsorbate | Parameters studied | Findings | Software used | author |
---|---|---|---|---|---|---|
1 | Computational Fluid Dynamics Analysis of Mercury Adsorption by Inverse-Vulcanized Porous Sulfur Copolymers | porous sulfur copolymers | mercury-ion concentrations, volumetric flow rate, temperature, and adsorbent thickness | The CFD model results are validated with the experimental results at fixed and varied operational conditions. The inverse-vulcanized sulfur present high porosity of (59.09%), less density (0.53 g/cm3), and smaller particle size (20−50 μm). Therefore, it exhibits high adsorption efficiency in the case of experimental (244 μg/g) and CFD simulations (249 μg/g) compared to other samples. | ANSYS FLUENT | [54] |
2 | Investigation of an Adsorptive Indigo Carmine Dye Removal via Packed Bed Column: Experiments and Computational Fluid Dynamics Simulation | graphene nanoadsorbent/Indigo Carmine Dye | The effect of flow rate, initial concentration, bed depth and reusability of the adsorbent were studied | Their result shows that High bed depth, low flow rate and high initial dye concentration were the potential parameters for the high adsorption capacity. The removal efficiency of indigo carmine dye was achieved to be 67% as flow rate, bed depth, and concentration of 1 ml/min, 28 cm and 10 ppm, respectively | CFD (using comsol Multiphysics) | [57] |
3 | Adsorption of methylene blue dye from the aqueous solution via bio-adsorption in the inverse fluidized-bed adsorption column using the torrefied rice husk | torrefied rice husk/methylene blue dye | Inverse fluidized bed bio-adsorption column has increased the overall methylene blue removal to 84% at saturation time of 95 min continuous adsorption, breakthrough time of 22 min and adsorptive capacity of 6.82 mg/g which is higher than those obtained from fixed bed adsorption column | - | [7] | |
4 | Combination of adsorption-diffusion model with CFD for study of desulfurization in fixed bed | Ag-TiO2-SiO2) / (4,6-DMDBT) | feed concentration, feed rate and column height | The results of their simulation demonstrated that the simulated results aren’t affected by the mesh number. Also, the mass transfer rate increases with increasing feed concentration at the beginning due to the higher driving force at higher feed concentration | Fluent software integrated in Ansys | [58] |
5 | Modelling and simulation of fixed bed adsorption column using integrated CFD approach | CO2/CH4 and CO2 moisture | Effect of feed velocity, bed porosity, feed concentration and temperature profile were studied | The simulated results were compared with experimental data and found to give a good agreement with error less than 2.5%. their result also showed that higher feed velocity tends to give a reduction in removal efficiency, also, the influence of hydrodynamics is more dominant as compared to the effect of mass transfer | [59] | |
6 | Isotherm and computational fluid dynamics analysis of nickel ion adsorption from aqueous solution using activated carbon | Activated carbon/ nickel | Adsorbent amount, feed flow rate, Ni2+ concentration, temperature, and solution pH on the removal efficiency as well as breakthrough and saturation points. | The result showed that > 99.0% removal of Ni+2 was obtained at the optimum conditions which are feed flow rate 5 mL/min, pH = 7.0, initial concentration = 5 mL/L, Temperature = 35 °C, and bed height 12 cm for the first 185 (± 5) minutes. | Comsol multiphysics | [60] |
7 | A Combined CFD-RSM Approach for Simulation and Optimization of Arsenic Removal in a Fixed Bed Adsorption Column | Iron ore/ arsenic | adsorbent bed depth, the feed flow rate, and the initial Arsenic concentration (conc.). response for RSM model are removal efficiency and the bed saturation time | The RSM predicted values were closed to the CFD measurement. Feed flowrate and bed depth were found to be more significant. Optimum conditions were found to be at bed height of 80 cm, the initial Arsenic concentration of 2.7 mmol/m3, and the feed flow rate of 1 L/min | CFD (Comsol Multiphysics) and RSM (Design expert 8) | [61] |
8 | Modeling and computational fluid dynamic simulation of acetaminophen adsorption using sugarcane bagasse | Sugarcane bagasse/ acetaminophen | Three experimental tests were carried out at 2.5 mL/min of flow rate, 57 mg/L of ACT concentration, and bed heights of 23, 33, and 43 cm. | The predicted model agreed with the experimental at r2 value of >0.91. the maximum error between experimental and predicted points was 7.03%. | COMSOL Multiphysics V5.4 | [41] |
Particular | Batch adsorption | Continuous fixed bed sorption | Continuous moving bed sorption | Continuous fixed bed sorption | Pulsed bed sorption |
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Introduction | Adsorbent and adsorbate are well mixed in diluted solution at constant volume in well mixed system | Fixed bed system consist of an adsorbent in which adsorbate is continuously flowing through a bed of adsorbent at constant rate | CMBS is steady state system where both adsorbent and adsorbate are in motion, and bed of adsorbent section remains constant but not in equal condition. | In this sorption, adsorbate is in contact with fluidized bed of adsorbent with sufficient or insufficient flow | In pulsed bed sorption, adsorbate is contacted with same adsorbent in bed, until desired results are not achieved. |
Features | Very easy and cheap technique. Most often researchers are using this technique to analyze feasibility of adsorbent adsorbate system | Very easy and cheap technique Used for higher quality of waste water having high pollution load. Also used for industrial purpose, because the adsorbate is continuously in contact with a given quantity of fresh adsorbent in fixed bed column system | Complicated and very expensive technique. As adsorbent is continuously replaced and fresh adsorbent is constantly contact with adsorbate. | Complicated and very expensive technique. Used for high quantity of waste water having high pollution load. Applicable for industries because it allows rapid mixing of adsorbent adsorbate since the flow is continuous and automated with controlled operation/easy handling | Very easy and cheap technique. It is very easily controlled and automatically operated system. Also it required lower dosage of adsorbent because the adsorbents were kept for regeneration after saturation. |
Disadvantages | Used for small quantity of waste water having minimum pollution load, therefore hardly found in industrial application. Adsorbent is removed from the system by simple filtration method | The problems here is adsorbent attrition, feed channeling, and non –uniform flow of adsorbent particles Forceful interaction is conducted here to reduce space and time. therefore, difficult to carry out a priori design and optimization of fixed bed columns without a quantitative approach | The large amount of adsorbents is required to complete sorption Continuous regeneration of adsorbent storage is essential | Flow of adsorbate is not measured with large deviation from plug flow and bubbling or feed channeling, which leads to insufficient contact of adsorbent adsorbate The rapid mixing of adsorbent adsorbate system leads to non-uniform residence time | Used for small quantity of waste water having minimum pollution load especially lower suspected solid Adsorbent is not unfilled in normal operation |
CFD | Conputational Fluid Dynamics |
ANN | Arificial Neural Network |
RSM | Response Surface Methodology |
MB | Methylene Blue |
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APA Style
Richard, O. U., Effiong, E. V., Asukwo, A. J., Antia, A. E., Onyejekwe, C. U. (2025). An Integrated Approach of ANN and CFD for Predicting and Modelling the Adsorptive Removal of Methylene Blue Dye Using Sandbox Seed as Adsorbent: A Review. Journal of Energy, Environmental & Chemical Engineering, 10(2), 56-67. https://doi.org/10.11648/j.jeece.20251002.12
ACS Style
Richard, O. U.; Effiong, E. V.; Asukwo, A. J.; Antia, A. E.; Onyejekwe, C. U. An Integrated Approach of ANN and CFD for Predicting and Modelling the Adsorptive Removal of Methylene Blue Dye Using Sandbox Seed as Adsorbent: A Review. J. Energy Environ. Chem. Eng. 2025, 10(2), 56-67. doi: 10.11648/j.jeece.20251002.12
AMA Style
Richard OU, Effiong EV, Asukwo AJ, Antia AE, Onyejekwe CU. An Integrated Approach of ANN and CFD for Predicting and Modelling the Adsorptive Removal of Methylene Blue Dye Using Sandbox Seed as Adsorbent: A Review. J Energy Environ Chem Eng. 2025;10(2):56-67. doi: 10.11648/j.jeece.20251002.12
@article{10.11648/j.jeece.20251002.12, author = {Obot Utibemfon Richard and Etuk Victor Effiong and Adam Joshua Asukwo and Antia Emem Antia and Chukwuemeka Uchenna Onyejekwe}, title = {An Integrated Approach of ANN and CFD for Predicting and Modelling the Adsorptive Removal of Methylene Blue Dye Using Sandbox Seed as Adsorbent: A Review }, journal = {Journal of Energy, Environmental & Chemical Engineering}, volume = {10}, number = {2}, pages = {56-67}, doi = {10.11648/j.jeece.20251002.12}, url = {https://doi.org/10.11648/j.jeece.20251002.12}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.jeece.20251002.12}, abstract = {The relevance application of dye cannot be overemphasized in our vicinity today, ranging from paintings, textiles, artistic purposes. Also, several other industrial applications including the cosmetics, leather, paper and even food industry. Notwithstanding its wide application, research has shown that the production of waste water containing synthetic dyes are deleterious to the environment and the ecosystem and therefore needs to be removed for the safety of the ecosystem. Several techniques like reverse osmosis, membrane filtration and coagulation can be used for removal of dyes. Some of these methods, despite their efficiency in wastewater treatment, they are expensive and sometimes complex to set up, therefore there is need for cheaper, affordable and simple method of wastewater treatment. Adsorption, mostly with waste biomass has proven to be a good and inexpensive method of dye removal from waste water. Therefore, this article reviewed adsorption of methylene blue dye unto sandbox seed biosorbent in a fixed bed continuous adsorption column. This review shows that there is still more to be done in terms of combining two or more different approaches in predicting and modelling adsorption of methylene blue removal from effluent water in order to obtain optimum result from treated water. }, year = {2025} }
TY - JOUR T1 - An Integrated Approach of ANN and CFD for Predicting and Modelling the Adsorptive Removal of Methylene Blue Dye Using Sandbox Seed as Adsorbent: A Review AU - Obot Utibemfon Richard AU - Etuk Victor Effiong AU - Adam Joshua Asukwo AU - Antia Emem Antia AU - Chukwuemeka Uchenna Onyejekwe Y1 - 2025/06/25 PY - 2025 N1 - https://doi.org/10.11648/j.jeece.20251002.12 DO - 10.11648/j.jeece.20251002.12 T2 - Journal of Energy, Environmental & Chemical Engineering JF - Journal of Energy, Environmental & Chemical Engineering JO - Journal of Energy, Environmental & Chemical Engineering SP - 56 EP - 67 PB - Science Publishing Group SN - 2637-434X UR - https://doi.org/10.11648/j.jeece.20251002.12 AB - The relevance application of dye cannot be overemphasized in our vicinity today, ranging from paintings, textiles, artistic purposes. Also, several other industrial applications including the cosmetics, leather, paper and even food industry. Notwithstanding its wide application, research has shown that the production of waste water containing synthetic dyes are deleterious to the environment and the ecosystem and therefore needs to be removed for the safety of the ecosystem. Several techniques like reverse osmosis, membrane filtration and coagulation can be used for removal of dyes. Some of these methods, despite their efficiency in wastewater treatment, they are expensive and sometimes complex to set up, therefore there is need for cheaper, affordable and simple method of wastewater treatment. Adsorption, mostly with waste biomass has proven to be a good and inexpensive method of dye removal from waste water. Therefore, this article reviewed adsorption of methylene blue dye unto sandbox seed biosorbent in a fixed bed continuous adsorption column. This review shows that there is still more to be done in terms of combining two or more different approaches in predicting and modelling adsorption of methylene blue removal from effluent water in order to obtain optimum result from treated water. VL - 10 IS - 2 ER -