SinoGreenTech Academic Portal
Open AccessDOI: 10.12030/j.cjee.202511054Original Research

S-scheme Bi6O5(OH)3(NO3)5·3H2O/BiOBr0.8I0.2 Heterojunction Photocatalyst: Synthesis and Visible-Light Degradation Mechanism of Rhodamine B

School of Civil and Transportation Engineering, Guangdong University of Technology, Guangzhou 510006, China

Read Executive PreviewQuick FAQ
S-scheme Bi6O5(OH)3(NO3)5·3H2O/BiOBr0.8I0.2 Heterojunction Photocatalyst: Synthesis and Visible-Light Degradation Mechanism of Rhodamine B
Graphical Abstract / Figure
Published In
Chinese Journal of Environmental Engineering
Published:January 15, 2026Edition:Vol. 20, Issue 7 • pp. 100-112Citation:LI Dongmei et al. (2026), Chinese Journal of Environmental Engineering
Impact FactorPeer-Reviewed Core
Source Journal环境工程学报

Key Takeaways & Executive Findings

  • • • Optimal mass ratio (BON:BI = 2:8) yields BON@BIOPT with 99.8% RhB degradation in 30 min visible light, a 1.9-fold improvement over pristine BI (52.2%), and an apparent rate constant (Kapp) of 0.20617 min⁻¹—8.64 times higher than BI (0.02385 min⁻¹). This performance leap addresses the bottleneck of slow kinetics in single-phase photocatalysts, enabling faster treatment cycles in industrial wastewater. • • BON@BIOPT exhibits a 37.4% increase in specific surface area (44.7 vs. 32.54 m²·g⁻¹) and a 20 nm red-shift in absorption edge (580 vs. 560 nm), narrowing the bandgap from 2.55 to 2.43 eV. Enhanced light harvesting and more active sites directly translate to higher quantum efficiency and lower energy consumption for visible-light-driven water treatment. • • The S-scheme heterojunction with internal electric field suppresses charge recombination, as evidenced by the dominant reactive species (O₂•⁻ and h⁺). This mechanistic design ensures efficient spatial separation of redox-active carriers, a critical factor for achieving sustained high mineralization rates in complex effluents. • • BON@BIOPT retains 88.6% degradation efficiency after 7 cycles and maintains 85–98% efficiency under pH variations and in the presence of common anions (HCO₃⁻, Cl⁻, SO₄²⁻, H₂PO₄⁻, NO₃⁻). This robustness indicates operational longevity and resilience to real-world water matrices, reducing catalyst replacement frequency and operational costs.

Abstract

A novel S-scheme heterojunction photocatalyst, Bi6O5(OH)3(NO3)5·3H2O/BiOBr0.8I0.2 (BON@BI), was synthesized via a one-step hydrothermal method using Bi6O5(OH)3(NO3)5·3H2O (BON), KBr, and KI as precursors. The mass ratio of BON to BiOBr0.8I0.2 (BI) was optimized, revealing that the 20% BON@BI composite (BON@BIOPT) exhibited the highest visible-light photocatalytic activity. Under 30 min of visible-light irradiation, BON@BIOPT achieved a 99.8% degradation efficiency of Rhodamine B (RhB), approximately twice that of pristine BI (52.2%). The composite displayed a rod-like morphology with uniform nanosheets, and its specific surface area increased from 32.54 m²·g⁻¹ (BI) to 44.7 m²·g⁻¹. The absorption edge red-shifted from 560 nm (BI) to 580 nm, narrowing the bandgap from 2.55 eV to 2.43 eV. The S-scheme heterojunction formed between BON and BI generates an internal electric field that effectively suppresses recombination of strongly reducing photogenerated electrons and strongly oxidizing holes, with superoxide radicals (O₂•⁻) and holes (h⁺) identified as the primary reactive species. BON@BIOPT exhibited excellent stability, retaining 88.6% degradation efficiency after seven consecutive cycles. It also demonstrated robust environmental adaptability, maintaining 85–98% degradation efficiency under various pH conditions and in the presence of interfering anions. The degradation pathway of RhB involves N-de-ethylation, cleavage of the conjugated chromophore, and deamination, ultimately mineralizing into low-molecular-weight organics, inorganic salts, CO₂, and H₂O. These results underscore the potential of BON@BIOPT for practical remediation of organic pollutants in water.

1. Introduction

Conventional semiconductor photocatalysts, such as TiO₂, suffer from wide bandgaps (ca. 3.2 eV) that restrict photoactivation to the UV region, limiting solar energy utilization to less than 5% of the solar spectrum. Moreover, rapid recombination of photogenerated electron-hole pairs and low specific surface areas result in poor quantum yields and slow degradation kinetics, rendering them economically unviable for large-scale water treatment. Bismuth oxyhalides (BiOX, X=Cl, Br, I) have emerged as promising visible-light-active alternatives due to their layered structures and tunable bandgaps, yet pure BiOX phases still exhibit moderate activity and stability. For instance, BiOBr0.8I0.2, a solid solution with an optimal bandgap of 2.55 eV, degrades only 52.2% of RhB in 30 minutes, underscoring the need for further enhancement.

This study addresses these limitations by constructing an S-scheme heterojunction between Bi6O5(OH)3(NO3)5·3H2O (BON) and BiOBr0.8I0.2 (BI). BON, a bismuth subcarbonate with a unique cage-like structure, can be transformed in situ into heterojunctions via anion exchange, facilitating intimate interfacial contact. The resulting BON@BI heterojunction leverages the internal electric field to promote spatial separation of photogenerated carriers, while the solid solution component extends visible-light absorption. This synergistic design achieves a 99.8% degradation of RhB in 30 minutes, representing a significant advancement over single-component photocatalysts and offering a viable route for efficient, stable, and environmentally adaptable water purification technologies.

SinoTechIntel Interactive Document Reader
Page 1–5 of Preview
100%
Download Full PDF

Loading authentic research manuscript (Pages 1–5)...

Cite This Research Paper
LI Dongmei, HE Shuai, JIANG Shuxian, CHEN Zhixiang, WU Hanjie, ZHANG Jinming, DAI Ziqiang, LIU Ziye (2026). S-scheme Bi6O5(OH)3(NO3)5·3H2O/BiOBr0.8I0.2 Heterojunction Photocatalyst: Synthesis and Visible-Light Degradation Mechanism of Rhodamine B. Chinese Journal of Environmental Engineering. https://doi.org/10.12030/j.cjee.202511054
SinoGreenTech Academic & Legal Disclaimer

Research & Educational Purpose Only: The translations, structured abstracts, analytical annotations, and data reports provided by SinoGreenTechare intended exclusively for academic research, internal corporate R&D, and educational benchmarking. They do not constitute formal engineering, chemical safety, legal, or professional advice.

Copyright & Intellectual Property Notice: Original copyright of the underlying source articles and experimental data remains with the respective authors, institutions, and original publishing journals. SinoGreenTech claims intellectual property only over its proprietary translations, analytical syntheses, and AEO structured enhancements in accordance with international fair use and academic citation principles.

Frequently Asked Questions

What is the long-term operational stability of BON@BIOPT under continuous flow conditions, and how does it compare to slurry batch reactors?

The catalyst retains 88.6% degradation efficiency after 7 consecutive batch cycles, indicating good reusability. However, continuous flow operation may introduce mechanical attrition and catalyst loss. The rod-like morphology with uniform nanosheets (44.7 m²·g⁻¹) suggests potential for immobilization on supports, but further studies on long-term stability under hydrodynamic stress are required. The current data support batch applications, with scale-up needing careful consideration of reactor design to minimize catalyst washout.

What is the cost breakdown for synthesizing BON@BIOPT compared to commercial TiO₂ (P25), and does the enhanced performance justify the premium?

Precise cost data are not provided, but the synthesis uses inexpensive precursors (Bi(NO₃)₃·5H₂O, KBr, KI) and a simple hydrothermal method, which is scalable. P25 costs roughly $20–50/kg, while bismuth-based catalysts are typically more expensive due to bismuth salt costs. However, the 99.8% degradation in 30 minutes versus P25's negligible visible-light activity justifies the premium for applications requiring visible-light or solar-driven processes. A techno-economic analysis is recommended to quantify lifecycle costs.

How does the catalyst perform under real sunlight conditions, and what is the quantum efficiency (QE) at specific wavelengths?

The study used a visible-light source (likely λ>420 nm), but actual solar QE was not measured. The absorption edge at 580 nm suggests utilization of up to ~580 nm, covering a significant portion of the solar spectrum. To estimate solar-to-chemical efficiency, one would need to measure apparent quantum yield (AQY) at monochromatic wavelengths. The Kapp of 0.20617 min⁻¹ under visible light is promising, but outdoor testing is essential to validate performance under varying light intensities.

What are the degradation intermediates of RhB, and are they toxic? The paper mentions N-de-ethylation and chromophore cleavage, but are the final products fully mineralized?

The study indicates that RhB is degraded via N-de-ethylation, cleavage of the conjugated chromophore, and deamination, ultimately mineralizing into low-molecular-weight organics, inorganic salts, CO₂, and H₂O. However, detailed intermediate identification (e.g., via LC-MS) is not provided. While complete mineralization is claimed, the presence of partially oxidized intermediates cannot be ruled out. Toxicity assays (e.g., Microtox) are recommended to ensure the effluent is non-toxic.

How does the presence of natural organic matter (NOM) affect the degradation efficiency, and can the catalyst be regenerated after fouling?

The study tested common inorganic anions (HCO₃⁻, Cl⁻, SO₄²⁻, H₂PO₄⁻, NO₃⁻) and found degradation efficiencies of 85–98%, indicating good tolerance. However, NOM, which is ubiquitous in natural waters, can scavenge reactive species and absorb light, potentially reducing efficiency. The catalyst's stability over 7 cycles suggests some resistance to fouling, but regeneration protocols (e.g., washing with dilute acid or UV irradiation) have not been reported. Further studies with NOM-spiked solutions are necessary.

Related Chinese Research & Cross-Citations

Research Citation2026
Analysis of National and Local Policies for Medical Waste Treatment and Disposal in China

Analysis of National and Local Policies for Medical Waste Treatment and Disposal in China

The escalating generation of medical waste, driven by healthcare expansion and frequent medical activities, poses significant environmental and public health risks. Under the framework of ecological civilization, China is developing a comprehensive policy system for medical waste treatment and disposal, yet the current framework remains nascent and exhibits inconsistencies between national and local policies. This study systematically analyzes the status of national and local policies from 2003 to 2024, collecting 413 policy documents (166 from national ministries and 247 from provincial governments). The analysis examines temporal evolution, regional distribution, and policy focus, alongside the influence of medical waste output, treatment technologies, facility infrastructure, and major epidemic responses. Findings reveal distinct policy phases: initial self-disposal, exploratory management, foundational system building, and rapid development. Regional disparities are pronounced, with eastern coastal areas showing more advanced policies due to greater technical and financial resources. The surge in medical waste, particularly during the COVID-19 pandemic, underscores the need for enhanced regulatory guidance. Non-incineration technologies are gaining traction for their environmental and cost benefits, and facility coverage has improved but remains uneven. The study proposes five policy principles to foster technological innovation and industrial upgrading, ensuring safe medical waste management and environmental protection.

Examine Full Data & PDF
Research Citation2026
Kinetic Analysis and Simulation of Pollutant Removal in Sewage Networks

Kinetic Analysis and Simulation of Pollutant Removal in Sewage Networks

This study investigates pollutant removal characteristics and kinetic behaviors in sewage networks, and analyzes their impact on the carbon-to-nitrogen ratio (C/N, as COD/TN) of influent to wastewater treatment plants. Source water quality sampling at drainage outlets revealed spatial and temporal variations in C/N, with domestic sewage exhibiting higher C/N than industrial sewage, and diurnal peaks reaching 6.92 versus 4.71 during off-peak hours. Using a pilot-scale adjustable sewage network system in Kunshan, experiments were conducted under high (0.491 m·s−1) and low (0.089 m·s−1) flow velocities, monitoring pollutant removal over 144 hours. Pseudo-first-order kinetics were applied to model COD and TN removal. Results showed that COD (including SCOD and PCOD), BOD5, and SS achieved approximately 80% removal within 144 h, with higher removal at low flow velocity. TN, NH3-N, and TP exhibited lower overall removal rates. Kinetic fitting revealed that COD removal rate constants (kCOD) were significantly higher than those for TN (kTN), and both decreased with increasing flow velocity: at low velocity, kCOD=0.0167 h−1 and kTN=0.0029 h−1; at high velocity, kCOD=0.0127 h−1 and kTN=0.0020 h−1. Simulations based on actual source pollutant concentrations indicated that the time for C/N to drop to the denitrification critical value of 4.50 was 12.24 h at high velocity, but shortened to 9.49 h at low velocity. These findings demonstrate that increasing flow velocity effectively retards the decline of C/N. Therefore, regulating network flow velocity to reduce hydraulic retention time is a key strategy for maintaining adequate C/N at the terminal and ensuring denitrification efficiency in wastewater treatment plants.

Examine Full Data & PDF
Research Citation2026
Preparation of Trimetallic-Carbon Composite Catalysts and Their Application in Catalytic Ozonation of Industrial Wastewater

Preparation of Trimetallic-Carbon Composite Catalysts and Their Application in Catalytic Ozonation of Industrial Wastewater

Advanced oxidation processes (AOPs) are promising for degrading organic pollutants in water treatment. Heterogeneous catalytic ozonation (HCO) has gained attention due to its high oxidation efficiency, strong interference resistance, and low secondary pollution. In this study, a series of trimetallic-carbon composite ozone catalysts were prepared via an organic precursor calcination method using γ-Al2O3 as support. This method enhanced catalytic activity and mechanical strength while overcoming the limitations of carbon materials (low mechanical strength) and metal-based materials (poor mass transfer). The optimized catalyst, CA-FeCoCu, comprising Fe, Co, Cu, carbon, and alumina, exhibited excellent performance in phenol degradation and real industrial wastewater treatment. Characterization revealed that the synergistic effect of trimetals and the introduction of multiple carbon types increased specific surface area and hydroxyl radical (·OH) generation. In a pilot-scale fixed-bed reactor, the CA-FeCoCu/O3 system reduced COD from 120 mg·L−1 to below 40 mg·L−1, with an O3 consumption ratio (O/C) of less than 1, effectively lowering operational costs. This work provides a new strategy for developing efficient and stable heterogeneous O3 catalysts and offers a reference for the practical application of HCO in industrial wastewater treatment.

Examine Full Data & PDF
Research Citation2026
Differentiated Characteristics of Suspended Particulate Matter and Their Effects on Water Quality in the Middle and East Routes of the South-to-North Water Diversion Project

Differentiated Characteristics of Suspended Particulate Matter and Their Effects on Water Quality in the Middle and East Routes of the South-to-North Water Diversion Project

This study investigates the spatiotemporal differentiation of suspended particulate matter (SPM) characteristics, sources, and their impacts on water quality between the Middle Route (closed artificial channel) and East Route (open natural water system) of the South-to-North Water Diversion Project. Thirty sampling sites (13 on the Middle Route, 17 on the East Route) were established, and samples were collected during dry and wet seasons. Water quality parameters and SPM characteristics were analyzed, including particle size distribution, total suspended solids (TSS), chlorophyll a, and stable carbon and nitrogen isotopes. Results show that the Middle Route maintains good and stable water quality, with SPM dominated by coarse particles (>63 μm, 61.43%–94.68%), total phosphorus (TP) <0.01 mg·L−1, and a significant positive correlation between chlorophyll a and coarse particles (r=0.60), indicating algal aggregation dominates particle formation. In contrast, the East Route exhibits high and fluctuating nitrogen and phosphorus concentrations, with SPM dominated by fine particles (<20 μm, 51.26%–88.61%), TP ranging from 0.03 to 1.11 mg·L−1, and a positive correlation with fine particles, suggesting significant external inputs. Carbon and nitrogen isotope analysis reveals that Middle Route SPM primarily originates from autochthonous algae (contribution >46.75%), while East Route SPM is influenced by both terrestrial C3 plants and algae. The distinct engineering and management approaches of the two routes lead to significant differences in SPM characteristics and sources, thereby affecting water quality dynamics. The Middle Route requires an 'algal reduction and hydrodynamic optimization' strategy to control algal-derived coarse particle deposition, whereas the East Route benefits from 'retention-sedimentation and wetland purification' to reduce external fine particles and pollutant inputs. This research provides theoretical support and practical guidance for differentiated SPM management in long-distance water diversion systems.

Examine Full Data & PDF
Research Citation2026
Combined Ozone Micro-Nano Bubble Oxidation and Powdered Activated Carbon Adsorption for Removal of Taste and Odor Compounds from Drinking Water

Combined Ozone Micro-Nano Bubble Oxidation and Powdered Activated Carbon Adsorption for Removal of Taste and Odor Compounds from Drinking Water

Algal-derived taste and odor compounds (2-methylisoborneol, 2-MIB, and geosmin, GSM) in drinking water sources are poorly removed by conventional treatment. This study systematically evaluated the standalone and combined performance of ozone micro-nano bubbles (O3-MNBs) oxidation and powdered activated carbon (PAC) adsorption for removing 2-MIB, GSM, and algal cells from source water. Results showed that O3-MNBs pre-oxidation achieved >97.5% removal of odorants at 400 ng·L−1 and 67.2% algal cell removal within 30 min. When applied as a deep treatment stage, the degradation rate constant (k) was 10.1%–25.6% higher than in pre-oxidation due to lower background matrix interference. Both pre-oxidation and deep treatment reduced effluent concentrations of 2-MIB and GSM to below 10 ng·L−1, with oxidation kinetics fitting pseudo-first-order models (R²>0.95). PAC adsorption of both compounds followed pseudo-second-order kinetics (R²>0.99), with GSM equilibrium adsorption capacity approximately 20.0% higher than that of 2-MIB. In pure water, adsorption capacity increased by >10.0% compared to raw water. Based on kinetic models, a quantitative prediction method was established for O3-MNBs oxidation and PAC adsorption processes, aiming to achieve efficient odorant removal and cost optimization, providing theoretical support for advanced drinking water purification and smart water plant construction.

Examine Full Data & PDF
Research Citation2026
Pulsed Electric Field Enhancement of Nitrogen Removal Performance and Microbial Community Structure Response in Anammox Granular Sludge

Pulsed Electric Field Enhancement of Nitrogen Removal Performance and Microbial Community Structure Response in Anammox Granular Sludge

This study investigated the effects of a ring-shaped pulsed electric field (PEF) (1.5 V, 4 h on-time per cycle) on nitrogen removal performance and microbial community structure of anammox granular sludge (AnGS). Two anaerobic sequencing batch reactors (R1 control, R2 with PEF) were operated under stepwise increasing nitrogen loading rates (NLR). At NLR below 1,155 mg·(L·d)−1, R2 exhibited total nitrogen removal efficiency (TRE) 7.5%–17.0% higher than R1, with biomass, specific anammox activity (SAA), and extracellular polymeric substances (EPS) increased by 5%–7%, 21%–71%, and 54%–77%, respectively. However, at NLR above 1,320 mg·(L·d)−1, the toxic effect of nitrite dominated, and PEF enhancement diminished or even reversed to inhibition. Microbial community analysis revealed that at low-to-moderate NLR, PEF increased the relative abundance of Planctomycetes and key anammox bacteria (Candidatus Brocadia and Candidatus Jettenia), along with enhanced community richness (Chao1) and diversity (Shannon/Simpson indices). At high NLR, PEF decreased microbial richness compared to R1. Principal component analysis and redundancy analysis indicated that PEF was the key factor driving community differences at low-to-moderate NLR, whereas nitrite concentration became the dominant factor at high NLR. This study provides theoretical support for enhancing the resilience and engineering application of anammox processes.

Examine Full Data & PDF