Pub Date : 2026-06-01Epub Date: 2026-02-23DOI: 10.1016/j.cscee.2026.101351
Marco Gaibor-Pacheco , Suanny Mosquera-Romero
In membrane-based chlor-alkali processes, brine recirculation is essential for improving operational sustainability; however, sodium sulfate (Na2SO4) accumulation in the loop hinders chlorine production. This study evaluates an integrated treatment scheme combining chemical precipitation and nanofiltration (NF) to remove Na2SO4 and enhance effluent reuse in a chlor-alkali plant in Guayaquil, Ecuador. Laboratory precipitation tests using real industrial effluent examined the influence of calcium chloride (CaCl2) dosage, temperature, and pH. The best removal (49.3 ± 4.2% w/w) was achieved with 45 mL L−1 CaCl2 at 70 °C, pH 9-11, and 20 min of mixing, while efficiencies fell below 30% at 40-55 °C even with higher dosages (≥50 mL L−1). Full-scale NF trials showed 72.8% w/w Na2SO4 rejection at 25 bar with 67.9% w/w water recovery. Both treated effluents were suitable for reintegration into the brine circuit. Mass balance analysis indicated that the combined process recovers up to 81.3% of the effluent, equivalent to 8051 m3 year−1 of water and 1393 t year−1 of NaCl, while mitigating saline discharges. The estimated capital cost (11,7021 USD) is offset by annual raw material savings of 93,964 USD. Overall, integrating chemical precipitation with membrane separation enhances process circularity, reduces freshwater consumption, and mitigates environmental impacts, while ensuring economic viability.
在膜基氯碱工艺中,盐水再循环对于提高操作可持续性至关重要;然而,硫酸钠(Na2SO4)在循环中的积累阻碍了氯的产生。本研究评估了厄瓜多尔瓜亚基尔(Guayaquil)氯碱厂化学沉淀和纳滤(NF)相结合的综合处理方案,以去除Na2SO4并提高废水回用。使用实际工业废水进行的实验室沉淀试验检查了氯化钙(CaCl2)用量、温度和pH的影响。在70 °C、pH 9-11和混合20分钟时,45 mL L -1 CaCl2达到了最佳去除率(49.3 ± 4.2% w/w),而在40-55 °C时,即使使用更高的用量(≥50 mL L -1),效率也降至30%以下。全尺寸NF试验表明,在25 bar条件下Na2SO4的截除率为72.8%,水回收率为67.9%。两种处理过的废水都适合重新进入盐水循环。质量平衡分析表明,该组合工艺可回收高达81.3%的出水,相当于8051 m3 /年的水和1393 t /年的NaCl,同时减少了盐水排放。预计的资本成本(11,7021美元)被每年节省的93,964美元的原材料所抵消。总体而言,将化学沉淀与膜分离相结合可以增强工艺循环,减少淡水消耗,减轻环境影响,同时确保经济可行性。
{"title":"Integration of chemical precipitation and nanofiltration for sodium sulfate control and brine loop closure in a Chlor Alkali plant","authors":"Marco Gaibor-Pacheco , Suanny Mosquera-Romero","doi":"10.1016/j.cscee.2026.101351","DOIUrl":"10.1016/j.cscee.2026.101351","url":null,"abstract":"<div><div>In membrane-based chlor-alkali processes, brine recirculation is essential for improving operational sustainability; however, sodium sulfate (Na<sub>2</sub>SO<sub>4</sub>) accumulation in the loop hinders chlorine production. This study evaluates an integrated treatment scheme combining chemical precipitation and nanofiltration (NF) to remove Na<sub>2</sub>SO<sub>4</sub> and enhance effluent reuse in a chlor-alkali plant in Guayaquil, Ecuador. Laboratory precipitation tests using real industrial effluent examined the influence of calcium chloride (CaCl<sub>2</sub>) dosage, temperature, and pH. The best removal (49.3 ± 4.2% w/w) was achieved with 45 mL L<sup>−1</sup> CaCl<sub>2</sub> at 70 °C, pH 9-11, and 20 min of mixing, while efficiencies fell below 30% at 40-55 °C even with higher dosages (≥50 mL L<sup>−1</sup>). Full-scale NF trials showed 72.8% w/w Na<sub>2</sub>SO<sub>4</sub> rejection at 25 bar with 67.9% w/w water recovery. Both treated effluents were suitable for reintegration into the brine circuit. Mass balance analysis indicated that the combined process recovers up to 81.3% of the effluent, equivalent to 8051 m<sup>3</sup> year<sup>−1</sup> of water and 1393 t year<sup>−1</sup> of NaCl, while mitigating saline discharges. The estimated capital cost (11,7021 USD) is offset by annual raw material savings of 93,964 USD. Overall, integrating chemical precipitation with membrane separation enhances process circularity, reduces freshwater consumption, and mitigates environmental impacts, while ensuring economic viability.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101351"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384594","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-06-01Epub Date: 2026-03-03DOI: 10.1016/j.cscee.2026.101358
Ainhoa Unzurrunzaga , Leire Lorenzo , Ainhoa Aguirre , María Fernández , Yolanda Belaustegui
Electro-membrane technologies to salt splitting chemicals such as potassium formate generated during the electrochemical conversion of captured CO2 to obtain formic acid and potassium hydroxide represents a crucial pathway toward carbon neutrality and circular economy. The study demonstrated that the most effective configuration employed two cation exchange membranes (Nafion 324) to separate the anodic, cathodic and central compartments, with the feed solution circulated through the central compartment. This setup enabled potassium ions to migrate to the catholyte, where KOH was concentrated, while protons generated in the anodic compartment moved into the central compartment, maintaining an acidic pH (≈1) and allowing the concentration of formic acid. Optimal performance was achieved at 1500 A m−2 and a circulated charge of 0.6715 F, yielding up to 100 g L−1 of formic acid and 140 g L−1 of potassium hydroxide. Additionally, pervaporation using a PERVAP 4101 membrane successfully broke the formic acid–water azeotrope, reaching concentrations up to 90%. This is the first study that demonstrates the production of highly concentrated formic acid from captured CO2 by combining electrodialysis with monopolar membranes and pervaporation technologies.
电膜技术将捕获的二氧化碳在电化学转化过程中产生的甲酸钾等化学物质分解为甲酸和氢氧化钾,是实现碳中和和循环经济的重要途径。研究表明,最有效的配置是使用两个阳离子交换膜(Nafion 324)来分离阳极、阴极和中心隔间,进料溶液通过中心隔间循环。这种设置使钾离子迁移到阴极液中,在阴极液中KOH被浓缩,而在阳极室中产生的质子移动到中央室,保持酸性pH值(≈1),并允许甲酸的浓度。在1500 A m−2和0.6715 F的循环电荷条件下,甲酸的收率为100 g L−1,氢氧化钾的收率为140 g L−1。此外,使用perap 4101膜的渗透蒸发成功地打破了甲酸-水共沸物,达到了90%的浓度。这是第一个通过结合电渗析、单极膜和渗透蒸发技术,从捕获的二氧化碳中生产高浓度甲酸的研究。
{"title":"Electromembrane and pervaporation technologies for the production of highly concentrated formic acid from captured CO2 valorization","authors":"Ainhoa Unzurrunzaga , Leire Lorenzo , Ainhoa Aguirre , María Fernández , Yolanda Belaustegui","doi":"10.1016/j.cscee.2026.101358","DOIUrl":"10.1016/j.cscee.2026.101358","url":null,"abstract":"<div><div>Electro-membrane technologies to salt splitting chemicals such as potassium formate generated during the electrochemical conversion of captured CO<sub>2</sub> to obtain formic acid and potassium hydroxide represents a crucial pathway toward carbon neutrality and circular economy. The study demonstrated that the most effective configuration employed two cation exchange membranes (Nafion 324) to separate the anodic, cathodic and central compartments, with the feed solution circulated through the central compartment. This setup enabled potassium ions to migrate to the catholyte, where KOH was concentrated, while protons generated in the anodic compartment moved into the central compartment, maintaining an acidic pH (≈1) and allowing the concentration of formic acid. Optimal performance was achieved at 1500 A m<sup>−2</sup> and a circulated charge of 0.6715 F, yielding up to 100 g L<sup>−1</sup> of formic acid and 140 g L<sup>−1</sup> of potassium hydroxide. Additionally, pervaporation using a PERVAP 4101 membrane successfully broke the formic acid–water azeotrope, reaching concentrations up to 90%. This is the first study that demonstrates the production of highly concentrated formic acid from captured CO<sub>2</sub> by combining electrodialysis with monopolar membranes and pervaporation technologies.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101358"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384599","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-06-01Epub Date: 2026-02-16DOI: 10.1016/j.cscee.2026.101348
Ntaote David Shooto, Patience Mapule Thabede
This study investigated the sorption capacity of potato peels for the removal of phenol from aqueous solution. The adsorption capacities of untreated potato peels (UPP) and acid-treated potato peels (APP) were compared with acid-base treated potato peels (ABPP). Characterisation of UPP, APP and ABPP by FTIR, SEM and XRD indicated that the surfaces of the adsorbents contain functional groups such as –OH, –C–O–C and –C–O. SEM images showed that the morphology of the adsorbents changed due to different chemical activations. The XRD patterns of APP and ABPP exhibited sharper peaks and higher intensities than those of UPP. The maximum sorption capacity of phenol on UPP, APP and ABPP was observed at pH 7. Adsorption isotherms showed that the Freundlich model best fitted the data, indicating multilayer sorption. The coefficient values for the PSO model were more appropriate for the uptake of phenol on all adsorbents. ABPP exhibited a higher sorption capacity for the removal of phenol, with an uptake capacity of 54.96 mg/g compared to UPP and APP.
{"title":"Modification of waste potato peels by combined acid-base treatment and its adsorption performance for the removal of phenol","authors":"Ntaote David Shooto, Patience Mapule Thabede","doi":"10.1016/j.cscee.2026.101348","DOIUrl":"10.1016/j.cscee.2026.101348","url":null,"abstract":"<div><div>This study investigated the sorption capacity of potato peels for the removal of phenol from aqueous solution. The adsorption capacities of untreated potato peels (UPP) and acid-treated potato peels (APP) were compared with acid-base treated potato peels (ABPP). Characterisation of UPP, APP and ABPP by FTIR, SEM and XRD indicated that the surfaces of the adsorbents contain functional groups such as –OH, –C–O–C and –C–O. SEM images showed that the morphology of the adsorbents changed due to different chemical activations. The XRD patterns of APP and ABPP exhibited sharper peaks and higher intensities than those of UPP. The maximum sorption capacity of phenol on UPP, APP and ABPP was observed at pH 7. Adsorption isotherms showed that the Freundlich model best fitted the data, indicating multilayer sorption. The coefficient values for the PSO model were more appropriate for the uptake of phenol on all adsorbents. ABPP exhibited a higher sorption capacity for the removal of phenol, with an uptake capacity of 54.96 mg/g compared to UPP and APP.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101348"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384624","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-06-01Epub Date: 2026-03-07DOI: 10.1016/j.cscee.2026.101365
Nguyen Cong Manh , Nguyen Tri Quang Hung , Huynh Thi Ngoc Oanh , Yasushi Mori
Household-scale biochar systems are increasingly promoted for agricultural waste management and decentralized environmental applications; however, their design is often constrained by feedstock handling, material stability, and process simplicity rather than maximum functional performance. This study examines key design constraints in household-scale rice-straw biochar production, focusing on feedstock densification and particle-size selection under practical conditions. Rice straw was pyrolyzed in a household drum kiln with and without mechanical compression. Biochar yield, physicochemical properties, mechanical stability, and adsorption behavior were evaluated. Uncompressed rice-straw biochar showed poor structural integrity and fragmented during handling, preventing reproducible adsorption measurements. In contrast, compressed rice-straw biochar (BCRS) exhibited markedly improved yield and stability. At 400 °C for 2 h, BCRS achieved a mass yield of 66.7 ± 1.5%, compared with 31.6 ± 0.9% for uncompressed straw. Methylene blue adsorption showed clear particle-size dependence: finer particles enabled faster uptake, whereas coarser particles exhibited higher apparent capacity under batch conditions. These findings indicate that handling feasibility and material stability are primary design constraints, while adsorption performance serves as a secondary screening criterion in decentralized systems.
{"title":"Design constraints governing household-scale rice-straw biochar systems: The role of feedstock densification and particle-size selection","authors":"Nguyen Cong Manh , Nguyen Tri Quang Hung , Huynh Thi Ngoc Oanh , Yasushi Mori","doi":"10.1016/j.cscee.2026.101365","DOIUrl":"10.1016/j.cscee.2026.101365","url":null,"abstract":"<div><div>Household-scale biochar systems are increasingly promoted for agricultural waste management and decentralized environmental applications; however, their design is often constrained by feedstock handling, material stability, and process simplicity rather than maximum functional performance. This study examines key design constraints in household-scale rice-straw biochar production, focusing on feedstock densification and particle-size selection under practical conditions. Rice straw was pyrolyzed in a household drum kiln with and without mechanical compression. Biochar yield, physicochemical properties, mechanical stability, and adsorption behavior were evaluated. Uncompressed rice-straw biochar showed poor structural integrity and fragmented during handling, preventing reproducible adsorption measurements. In contrast, compressed rice-straw biochar (BCRS) exhibited markedly improved yield and stability. At 400 °C for 2 h, BCRS achieved a mass yield of 66.7 ± 1.5%, compared with 31.6 ± 0.9% for uncompressed straw. Methylene blue adsorption showed clear particle-size dependence: finer particles enabled faster uptake, whereas coarser particles exhibited higher apparent capacity under batch conditions. These findings indicate that handling feasibility and material stability are primary design constraints, while adsorption performance serves as a secondary screening criterion in decentralized systems.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101365"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384914","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
The watershed of the Delta of Ouémé is part of the southern coastal sedimentary basin of Benin. Economic development in this region is essentially based on farming, fishing, and livestock breeding, which are activities that may lead to environmental pollution, including both surface and groundwater pollution. The major aim of the study is to examine the quality of groundwater and to find out the likely sources of pollution in this watershed, using an isotope mixing model (MixSIAR). The methodology applied calls on classical hydrochemical approaches, Self-Organizing Map (SOM), and stable nitrate isotopes (15N;18O) (allowing more accurate discrimination of contamination sources compared to hydrochemical methods). Results demonstrated that the origins of nitrate in groundwater are mainly from manure and sewage and soil nitrogen nitrification. The Bayesian model estimated the contribution of each source and the results have shown that manure and sewage represent the dominant contributors to groundwater nitrate (75.2 % and 87.3 % in the Mio-Pliocene and the Quaternary aquifers, respectively). Then, groundwater pollution during both the dry and rainy periods was mainly due to anthropogenic activities. These results highlight some major implications: (i) groundwater pollution is mainly of anthropogenic origin, calling for better control of agricultural and domestic practices; (ii) the isotopic approach coupled with advanced statistical methods is an effective tool for distinguishing and quantififing pollution sources; and (iii) the study provides a scientific basis for strengthening aquifer protection policies, limiting nitrate-related health risks and promoting sustainable management of water resources.
{"title":"Groundwater hydrochemistry and identification of nitrate pollution sources in the Ouémé Delta (Southern-Benin) using dual isotopes (15N–NO3 and 18O–NO3) and a Bayesian isotope mixing model","authors":"Aoulatou Alassane Zakari , Kodjo Apelete Raoul Kpegli , Dadja-Toyou Masamaéya Gnazou , Abdoukarim Alassane , Bio Guidah Chabi , Fabrice Messan Amene Lawson , Nicaise Yalo , Daouda Mama , Moussa Boukari","doi":"10.1016/j.cscee.2025.101303","DOIUrl":"10.1016/j.cscee.2025.101303","url":null,"abstract":"<div><div>The watershed of the Delta of Ouémé is part of the southern coastal sedimentary basin of Benin. Economic development in this region is essentially based on farming, fishing, and livestock breeding, which are activities that may lead to environmental pollution, including both surface and groundwater pollution. The major aim of the study is to examine the quality of groundwater and to find out the likely sources of pollution in this watershed, using an isotope mixing model (MixSIAR). The methodology applied calls on classical hydrochemical approaches, Self-Organizing Map (SOM), and stable nitrate isotopes (<sup>15</sup>N;<sup>18</sup>O) (allowing more accurate discrimination of contamination sources compared to hydrochemical methods). Results demonstrated that the origins of nitrate in groundwater are mainly from manure and sewage and soil nitrogen nitrification. The Bayesian model estimated the contribution of each source and the results have shown that manure and sewage represent the dominant contributors to groundwater nitrate (75.2 % and 87.3 % in the Mio-Pliocene and the Quaternary aquifers, respectively). Then, groundwater pollution during both the dry and rainy periods was mainly due to anthropogenic activities. These results highlight some major implications: (i) groundwater pollution is mainly of anthropogenic origin, calling for better control of agricultural and domestic practices; (ii) the isotopic approach coupled with advanced statistical methods is an effective tool for distinguishing and quantififing pollution sources; and (iii) the study provides a scientific basis for strengthening aquifer protection policies, limiting nitrate-related health risks and promoting sustainable management of water resources.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101303"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145617556","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-06-01Epub Date: 2025-12-26DOI: 10.1016/j.cscee.2025.101321
Mostafa Khodakarami, Víctor R. Vásquez
Maintaining compliant chlorine residuals across water distribution networks is challenging because concentrations evolve under time-varying hydraulics, advective transport, and bulk and wall decay kinetics, while field monitoring is sparse. Physics-based simulators such as EPANET can represent these processes but require careful calibration and can be difficult to use for rapid, network-wide decision support, while purely data-driven models may violate basic transport and reaction constraints and often need dense measurements. This study develops a physics- and chemistry-informed graph neural network (GNN) that learns network-wide chlorine dynamics from hydraulic simulations while embedding domain features that represent connectivity, flow behavior, water age, and decay parameters. Two GNN architectures—a Graph Convolutional Network (GCN) and a Gated Graph Neural Network (GGNN)—are trained on features including pressure, demand, chlorine concentration, flow velocity, headloss, and decay coefficient that capture the system's hydraulic and chemical behavior. The approach is demonstrated on a subsection of Ward 4 in Reno, Nevada using a 240-h EPANET extended-period simulation dataset. Compared with a graph convolutional network baseline, the proposed GGNN improves predictive accuracy, reducing the mean absolute error from about 0.38 to 0.22 mg/L and the root mean square error from about 0.57 to 0.35 mg/L, while increasing coefficient of determination (R2) from about 0.93 to about 0.97. At a representative snapshot, results show that the GGNN significantly outperforms the GCN, achieving lower error and higher R2 (>0.99), due to its iterative message-passing mechanism that captures long-range dependencies. Both models generalize well across hydraulic conditions, enabling accurate virtual sensing for real-time chlorine monitoring in sparsely instrumented networks.
{"title":"Chlorine transport and decay analysis in water distribution systems using hydraulic simulation and physics- and chemistry-informed graph neural networks","authors":"Mostafa Khodakarami, Víctor R. Vásquez","doi":"10.1016/j.cscee.2025.101321","DOIUrl":"10.1016/j.cscee.2025.101321","url":null,"abstract":"<div><div>Maintaining compliant chlorine residuals across water distribution networks is challenging because concentrations evolve under time-varying hydraulics, advective transport, and bulk and wall decay kinetics, while field monitoring is sparse. Physics-based simulators such as EPANET can represent these processes but require careful calibration and can be difficult to use for rapid, network-wide decision support, while purely data-driven models may violate basic transport and reaction constraints and often need dense measurements. This study develops a physics- and chemistry-informed graph neural network (GNN) that learns network-wide chlorine dynamics from hydraulic simulations while embedding domain features that represent connectivity, flow behavior, water age, and decay parameters. Two GNN architectures—a Graph Convolutional Network (GCN) and a Gated Graph Neural Network (GGNN)—are trained on features including pressure, demand, chlorine concentration, flow velocity, headloss, and decay coefficient that capture the system's hydraulic and chemical behavior. The approach is demonstrated on a subsection of Ward 4 in Reno, Nevada using a 240-h EPANET extended-period simulation dataset. Compared with a graph convolutional network baseline, the proposed GGNN improves predictive accuracy, reducing the mean absolute error from about 0.38 to 0.22 mg/L and the root mean square error from about 0.57 to 0.35 mg/L, while increasing coefficient of determination (R<sup>2</sup>) from about 0.93 to about 0.97. At a representative snapshot, results show that the GGNN significantly outperforms the GCN, achieving lower error and higher R<sup>2</sup> (>0.99), due to its iterative message-passing mechanism that captures long-range dependencies. Both models generalize well across hydraulic conditions, enabling accurate virtual sensing for real-time chlorine monitoring in sparsely instrumented networks.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101321"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145924994","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Development of highly efficient photocatalysts for the degradation of persistent and recalcitrant malachite green (MG) dye remains a significant challenge. In this study, mesoporous α-Fe2O3 was synthesized by calcining MIL-100(Fe) and subsequently encapsulated within ZIF-8 to form α-Fe2O3/ZIF-8 (FZF) composites. The resulting heterostructures exhibited a high surface area (566 m2/g), a narrow band gap (∼2.0 eV), improved charge separation, and strong adsorption capacity. Among the samples, FZF-25 achieved 99.35 % removal of 150 ppm MG within 80 min under UV irradiation and maintained excellent stability over four cycles. These findings highlight a promising MOF-derived α-Fe2O3/ZIF-8 approach that enables synergistic adsorption–photocatalysis process.
{"title":"Synthesis of MIL-100(Fe) derived α-Fe2O3 for fabrication of α-Fe2O3/ZIF-8 as photocatalyst of malachite green degradation","authors":"Karelius Karelius , Ratna Ediati , Eko Santoso , Uripto Trisno Santoso , Nuhaa Faaizatunnisa , Rifdah Adya Salsabila , Marvin Horale Pasaribu , Retno Agnestisia","doi":"10.1016/j.cscee.2025.101320","DOIUrl":"10.1016/j.cscee.2025.101320","url":null,"abstract":"<div><div>Development of highly efficient photocatalysts for the degradation of persistent and recalcitrant malachite green (MG) dye remains a significant challenge. In this study, mesoporous α-Fe<sub>2</sub>O<sub>3</sub> was synthesized by calcining MIL-100(Fe) and subsequently encapsulated within ZIF-8 to form α-Fe<sub>2</sub>O<sub>3</sub>/ZIF-8 (FZF) composites. The resulting heterostructures exhibited a high surface area (566 m<sup>2</sup>/g), a narrow band gap (∼2.0 eV), improved charge separation, and strong adsorption capacity. Among the samples, FZF-25 achieved 99.35 % removal of 150 ppm MG within 80 min under UV irradiation and maintained excellent stability over four cycles. These findings highlight a promising MOF-derived α-Fe<sub>2</sub>O<sub>3</sub>/ZIF-8 approach that enables synergistic adsorption–photocatalysis process.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101320"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145925671","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
This research demonstrates the conversion of plastic waste, specifically LDPE and PE, into fuel oil using a pyrolysis process. The fuel produced was tested in a diesel engine connected to a 4-kW generator for smart grid power supply. Using a fixed-bed pyrolysis reactor, the process reduced the required operating temperature by 250–300 °C and achieved a plastic-to-oil conversion yield of 66.67%–75.52%. The produced pyrolysis oil showed physical properties close to standard diesel, with a density of 0.74941 g/cm3 and viscosity of 1.007 mm2/s, following ASTM standards. Its chemical composition included 80.98% carbon, 12.88% hydrogen, 0.21% nitrogen, and 5.93% oxygen, with a heating value of 36.46 kJ/kg. Economically, pyrolysis oil costs 20 baht/liter (0.57 USD), which is significantly cheaper than commercial diesel at 32.94 baht/liter (0.94 USD). While diesel oil showed higher engine efficiency (60.64%) compared to pyrolysis oil (49.41%), the study suggests that pyrolysis offers a promising solution for plastic waste management by producing a cost-effective, diesel-like alternative fuel suitable for energy applications.
{"title":"Plastic waste-derived fuel in diesel engine for 4 kW power generation supporting smart grid stabilization","authors":"Paitoon Laodee , Preecha Sriprapakhan , Sakda Somkun , Nuwong Chollacoop , Pisit Maneechot","doi":"10.1016/j.cscee.2026.101350","DOIUrl":"10.1016/j.cscee.2026.101350","url":null,"abstract":"<div><div>This research demonstrates the conversion of plastic waste, specifically LDPE and PE, into fuel oil using a pyrolysis process. The fuel produced was tested in a diesel engine connected to a 4-kW generator for smart grid power supply. Using a fixed-bed pyrolysis reactor, the process reduced the required operating temperature by 250–300 °C and achieved a plastic-to-oil conversion yield of 66.67%–75.52%. The produced pyrolysis oil showed physical properties close to standard diesel, with a density of 0.74941 g/cm<sup>3</sup> and viscosity of 1.007 mm<sup>2</sup>/s, following ASTM standards. Its chemical composition included 80.98% carbon, 12.88% hydrogen, 0.21% nitrogen, and 5.93% oxygen, with a heating value of 36.46 kJ/kg. Economically, pyrolysis oil costs 20 baht/liter (0.57 USD), which is significantly cheaper than commercial diesel at 32.94 baht/liter (0.94 USD). While diesel oil showed higher engine efficiency (60.64%) compared to pyrolysis oil (49.41%), the study suggests that pyrolysis offers a promising solution for plastic waste management by producing a cost-effective, diesel-like alternative fuel suitable for energy applications.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101350"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384600","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-06-01Epub Date: 2026-02-23DOI: 10.1016/j.cscee.2026.101352
Francesca Tagliaferri , Laura Gianola , Laize Nalli de Freitas , Ademir Prata , Marzio Invernizzi
Advances in odor impact assessment increasingly rely on accurate atmospheric dispersion modelling. In this context, odor emissions from open biofilters are commonly modelled as non-buoyant area sources, implicitly neglecting plume rise effects. However, the biological activity within biofilters generates heat, producing emissions warmer than ambient air and potentially inducing buoyancy-driven plume rise. This study investigates the influence of plume rise parameterization on odor dispersion modelling from open biofilters using the CALPUFF model. A series of simulations is performed considering different source configurations (point, area, and buoyant area), and plume rise algorithms (Briggs and numerical). Results show that neglecting plume rise, as typically done in the literature, leads to substantial overestimations of odor concentrations compared to the other investigated scenarios. Including buoyancy effects produces outcomes that appear more physically consistent and representative of real emission behaviour, with comparable results between point and buoyant area sources. Within the spectrum of available algorithms, the semi-empirical formulation is inherently limited by simplifying assumptions, while numerical approaches exhibit enhanced physical robustness as they are subject to fewer constraints. Overall, the findings emphasize the importance of accounting for buoyancy in modelling open biofilters and suggest that common simplifications may lead to overly conservative outcomes.
{"title":"Influence of plume rise parameterization on odor impact assessment: A case study of open biofilters","authors":"Francesca Tagliaferri , Laura Gianola , Laize Nalli de Freitas , Ademir Prata , Marzio Invernizzi","doi":"10.1016/j.cscee.2026.101352","DOIUrl":"10.1016/j.cscee.2026.101352","url":null,"abstract":"<div><div>Advances in odor impact assessment increasingly rely on accurate atmospheric dispersion modelling. In this context, odor emissions from open biofilters are commonly modelled as non-buoyant area sources, implicitly neglecting plume rise effects. However, the biological activity within biofilters generates heat, producing emissions warmer than ambient air and potentially inducing buoyancy-driven plume rise. This study investigates the influence of plume rise parameterization on odor dispersion modelling from open biofilters using the CALPUFF model. A series of simulations is performed considering different source configurations (point, area, and buoyant area), and plume rise algorithms (Briggs and numerical). Results show that neglecting plume rise, as typically done in the literature, leads to substantial overestimations of odor concentrations compared to the other investigated scenarios. Including buoyancy effects produces outcomes that appear more physically consistent and representative of real emission behaviour, with comparable results between point and buoyant area sources. Within the spectrum of available algorithms, the semi-empirical formulation is inherently limited by simplifying assumptions, while numerical approaches exhibit enhanced physical robustness as they are subject to fewer constraints. Overall, the findings emphasize the importance of accounting for buoyancy in modelling open biofilters and suggest that common simplifications may lead to overly conservative outcomes.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101352"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147384822","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
The growing need for sustainable alternatives to fossil-derived heating motivates the development of biomass-based thermal systems for waste valorization. This study designed and operated a continuous pyrolysis system integrated with an updraft gasifier-syngas burner, using wood pellets as a renewable heat source to convert fresh palm fruit bunches (FFB) into valuable bio-products. The system replaced LPG heating, enabled direct utilization of undried FFB, and enhanced operational scalability. Stable operation was achieved at 1078 °C with low CO (280 mg Nm−3) and particulate emissions (56 mg Nm−3). Pyrolysis at 500 °C yielded biochar (9.5 wt%, HHV 28.1 MJ kg−1, with 23 % carbon retention equivalent to 44.7 tCO2eq yr−1), pyrolysis oil (21.9 wt%), wood vinegar (40.0 wt%), and gases (28.6 wt%). Techno-economic analysis indicated a net profit of 4.08 EUR h−1 and a short payback period of 1.5–1.9 years. These findings demonstrate that the integrated biomass gasification-pyrolysis system offers a technically feasible and economically attractive solution for low-carbon conversion of palm residues into energy and carbon-rich materials.
{"title":"Continuous gasification-pyrolysis of fresh palm fruit bunches for biochar production and carbon sequestration","authors":"Nathawat Unsomsri , Pachara Koedthong , Sittinun Tawkaew , Songkran Wiriyasart , Sommas Kaewluan","doi":"10.1016/j.cscee.2025.101309","DOIUrl":"10.1016/j.cscee.2025.101309","url":null,"abstract":"<div><div>The growing need for sustainable alternatives to fossil-derived heating motivates the development of biomass-based thermal systems for waste valorization. This study designed and operated a continuous pyrolysis system integrated with an updraft gasifier-syngas burner, using wood pellets as a renewable heat source to convert fresh palm fruit bunches (FFB) into valuable bio-products. The system replaced LPG heating, enabled direct utilization of undried FFB, and enhanced operational scalability. Stable operation was achieved at 1078 °C with low CO (280 mg Nm<sup>−3</sup>) and particulate emissions (56 mg Nm<sup>−3</sup>). Pyrolysis at 500 °C yielded biochar (9.5 wt%, HHV 28.1 MJ kg<sup>−1</sup>, with 23 % carbon retention equivalent to 44.7 tCO<sub>2</sub>eq yr<sup>−1</sup>), pyrolysis oil (21.9 wt%), wood vinegar (40.0 wt%), and gases (28.6 wt%). Techno-economic analysis indicated a net profit of 4.08 EUR h<sup>−1</sup> and a short payback period of 1.5–1.9 years. These findings demonstrate that the integrated biomass gasification-pyrolysis system offers a technically feasible and economically attractive solution for low-carbon conversion of palm residues into energy and carbon-rich materials.</div></div>","PeriodicalId":34388,"journal":{"name":"Case Studies in Chemical and Environmental Engineering","volume":"13 ","pages":"Article 101309"},"PeriodicalIF":0.0,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145737497","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}