| Literature DB >> 31847211 |
Min Zhang1, Xiangchun Wang1, Long Yang1, Yangyang Chu1.
Abstract
Heavy metals contaminated sediment has become a worldwide environmental issue due to its great harm to human and aquatic organisms. Thus, economical, effective, and environmentally-friendly remediation technologies are urgently needed. Among which, combined remediation technologies have attracted widespread attention for their unique advantages. This paper introduces combined remediation technologies based on physical-, chemical-, and bio-remediation of heavy metal polluted sediments. Firstly, the research progress in physical-chemical, bio-chemical, and inter-organismal (including plants, animals, microorganisms) remediation of heavy metal polluted sediments are summarized. Additionally, the paper analyzes the problems of the process of combined remediation of heavy metals in river sediments and outlooks the future development trends of remediation technologies. Overall, this review provides useful technology references for the control and treatment of heavy metal pollution in river sediments.Entities:
Keywords: combined remediation technology; heavy metal pollution; sediment
Mesh:
Substances:
Year: 2019 PMID: 31847211 PMCID: PMC6950138 DOI: 10.3390/ijerph16245098
Source DB: PubMed Journal: Int J Environ Res Public Health ISSN: 1660-4601 Impact factor: 3.390
Combined electrokinetic remediation (EKR) technologies.
| Combined Remediation Technology | Principle | References |
|---|---|---|
| EKR-acidification | The acidic cleaning solution neutralizes the OH− produced by the cathode in the electrolytic cell, eliminates the sediment alkalinization phenomenon as well as prevents the precipitation of heavy metals, and finally improves the removal efficiency of heavy metals. | [ |
| EKR-flocculant | After the flocculant pretreatment, the sediment undergoes flocculation, resulting in mud–water separation. The porosity of sediment particles becomes larger, which provides channels for ion migration and improves the removal efficiency of heavy metals. | [ |
| EKR-bioleaching | The microbial activity and acid production during the biological leaching process transform the insoluble metal sulfide to soluble metal sulfate. With the assistance of EKR, the ion migration speed is accelerated and the removal efficiency is improved. | [ |
| EKR-permeable reactive barrier (PRB) | This technology combines the advantages of both EKR and the PRB. Under application of an electric field, metal ions react with the filling material in the PRB during the process of migration to the cathode, which stabilizes the heavy metal ions for further centralized processing. | [ |
| EKR-adsorption | Under the action of the electric field force, heavy metal ions migrate to a specific adsorption area, where in-situ removal of heavy metals is achieved by being adsorbed by an adsorbent. | [ |
| EKR-ion exchange membrane | Selective semi-permeable membranes are used to separate the electrodes from the contaminated soil/sediment, preventing the entry of OH− and H+, thereby avoiding the alkalization of the cathode and improving the repair efficiency. | [ |
Effect of leaching conditions on heavy metal removal.
| Heavy Metal | Condition Variable | Main Results | References |
|---|---|---|---|
| Hg, Cd, Cr, Pb, Zn, Ni | Eluent formulation ratio | When 2% hydrogen peroxide and 42% phosphoric acid were used to remove heavy metals from the remaining sludge, the heavy metal removal rates reached more than 90%. | [ |
| Cr | Eluent concentration, contact time, liquid/solid ratio, pH | When the treatment time was 1 h, the ethylenediaminetetraacetic acid (EDTA) concentration was 0.1 mol/L, the soil-liquid mass ratio was 1:10, and the pH was 5, the removal effect was the best. The removal rate of Cr reached as high as 22% and Cr6+ was 98.5%. | [ |
| Cu, Zn, Cr, Pb, Ni, Mn | Eluent concentration, contact time, liquid/solid ratio, pH | Contact time, liquid/solid ratio, and pH of washing agents had notable influence on removal efficiency. The optimal washing conditions were identified as: concentration of 8.0 g/L, contact time of 24 h, liquid/solid ratio of 20/1, and original pH of washing agent. | [ |
| Cu, Zn, Pb, Cd | Liquid/solid ratio, pH | When the molar mass ratios of ethylenediamine | [ |
| Pb, Cd | Eluent concentration, contact time, pH | With the increase of eluent concentration, the leaching efficiency of Pb and Cd generally showed an upward trend; as the pH of the eluent increased, the eluent rate generally decreased; as the eluent time increased, the eluent rate had three trends: (i) overall increase, (ii) first increase, then decrease, and (iii) no significant change. | [ |
Effects of ultrasound/microwave conditions on heavy metal removal.
| Heavy Metal | Influencing Factors | Main Results | References |
|---|---|---|---|
| Hg | Ultrasound action time | With the increase of the action time, desorption of Hg was firstly strengthened, but the rate was reduced when the time further increased. This was because the Al(OH)3 precipitating during ultrasonic process absorbed Hg. | [ |
| Cu | Sound intensity | When the ultrasonic wave with a frequency of 50 KHz was applied for 3 h, the repair effect was enhanced with the increase of the ultrasonic sound intensity; when the sound intensity reached 150 V, the enrichment ratio of Cu2+ increased by 43%. | [ |
| Cd, Pb, Cr | Water content of the sample | Under the action of ultrasound, the soil remediation effect was the best when the water content was 14%; when the water content further increased to 16%, the remediation effect was not significantly improved. | [ |
| Ge | Ultrasound action time, sound intensity | When the ultrasonic power was 700 W and reacted at 80 °C for 40 min, the leaching effect of Ge was the highest, reaching 92.7%. When the power continuously increased, the effect became worse. | [ |
| Cr, V | Ultrasound action time, sound intensity | When ultrasonic leaching was carried out at 60 °C for 60 min, the leaching rate of Cr and V reached the maximum. Ultrasonic assistance significantly reduced the reaction time and leaching temperature. | [ |