This study was conducted to understand the role of application sequence of pyrite and zero-valent iron (Fe) (simultaneous vs. sequential) on chromium (VI) removal by Fe. In batch experiments, pyrite and Fe were homogeneously mixed in batch reactors maintained at a constant total solids loading of 2 g L. In sequential batch experiments, however, the first reactor containing variable doses of pyrite was operated for 20 min, and the liquid fraction from the first reactor was then subsequently loaded into the second reactor containing a fixed Fe dose of 1.2 g L. The batch reactors achieved much higher Cr(VI) removal efficiency than sequential batch reactors under similar operating conditions due to discrepancies in Fe redox cycling activities between these two systems. In batch reactors, the Fe particles deposited on pyrite surface due to electrostatic attraction between negatively charged pyrite and positively charged Fe, thus, rendering the overall solids surface charge neutral at optimum pyrite and Fe doses. As a result, the whole system behaved like a composite material, with pyrite functioning as a support material for Fe. This stimulated Fe redox cycling more effectively to generate new Fe(II) sites on Fe for enhanced Cr(VI) removal relative to Fe only system. In sequential batch reactors, however, the Fe redox cycling activity was limited, but significantly increased with increasing pyrite dose in the first reactor. Overall, our results indicate that the stimulatory effect of pyrite on Cr(VI) removal by Fe may be much higher if the reactors are operated in batch mode.
Download full-text PDF |
Source |
---|---|
http://dx.doi.org/10.1016/j.jenvman.2022.115854 | DOI Listing |
Sci Rep
January 2025
Physical Science and Engineering Division, King Abdullah University of Science and Technology (KAUST), Thuwal, 23955, Saudi Arabia.
This study illuminates the mineral carbonation potential of zeolite minerals. Zeolite minerals are common alteration products of basaltic rocks and are known for their ability to rapidly exchange their interstitial cations with those in aqueous solutions. A series of closed system batch reactor experiments was conducted at 60 °C by combining stilbite, a Ca-bearing zeolite, with 0.
View Article and Find Full Text PDFThe present study demonstrates the significance of the C/N ratio and double helical ribbon (DHR) impeller in the anaerobic co-digestion (AnCo-D) of sugar refining process (SRP) effluent and molasses-based distillery spent wash (DSW) for improved biogas production. Both SRP & DSW were mixed in different percentages to achieve an optimum C/N ratio. Further biomethane potential analysis of mixed feeds with different C/N ratios was performed.
View Article and Find Full Text PDFPrep Biochem Biotechnol
January 2025
Environmental Technology Laboratory, Department of Biosciences and Bioengineering, Indian Institute of Technology Guwahati, Guwahati, India.
The study employed batch shake flasks to evaluate the impact of various nitrogen sources, phosphate levels, and sodium acetate (Na-acetate) on the growth and metabolite production. Adding Na-acetate to the medium resulted in significant improvements in critical metabolites. In shake flask experiments, this led to a cell dry weight (CDW) of 1.
View Article and Find Full Text PDFHeliyon
December 2024
Departments of Water Supply and Environmental Engineering, Arba Minch Water Technology Institute (AWTI), P. O. Box 21, Arba Minch, Ethiopia.
The sulfur-containing chemical warfare agents sulfur mustard HD and nerve agent VX are highly toxic and persistent in the environment. Therefore, their neutralisation requires harsh oxidation conditions, but also precise selectivity. Here we report the safe and effective detoxification of surrogates CEES and PhX by selective oxidation of the sulfur atom by generating peracetic acid from AcOEt and aq.
View Article and Find Full Text PDFEnter search terms and have AI summaries delivered each week - change queries or unsubscribe any time!