| Literature DB >> 35336185 |
Van Hong Thi Pham1, Jaisoo Kim2, Soonwoong Chang3, Woojin Chung3.
Abstract
Rapid industrialization has led to the pollution of soil and water by various types of contaminants. Heavy metals (HMs) are considered the most reactive toxic contaminants, even at low concentrations, which cause health problems through accumulation in the food chain and water. Remediation using conventional methods, including physical and chemical techniques, is a costly treatment process and generates toxic by-products, which may negatively affect the surrounding environment. Therefore, biosorption has attracted significant research interest in the recent decades. In contrast to existing methods, bacterial biomass offers a potential alternative for recovering toxic/persistent HMs from the environment through different mechanisms for metal ion uptake. This review provides an outlook of the advantages and disadvantages of the current bioremediation technologies and describes bacterial groups, especially extremophiles with biosorbent potential for heavy metal removal with relevant examples and perspectives.Entities:
Keywords: bacterial biomass; biosorbent; heavy metal removal; microbial metal removing strategy
Year: 2022 PMID: 35336185 PMCID: PMC8953973 DOI: 10.3390/microorganisms10030610
Source DB: PubMed Journal: Microorganisms ISSN: 2076-2607
Conventional methods for heavy metal removal.
| Methods | Description |
|---|---|
| Chemical precipitation | The most common method for heavy metal removal from solutions. The ionic metals are converted to insoluble forms by chemical reactions using precipitating reagents (precipitants) and form metal hydroxides, sulfides, carbonates, and phosphates (insoluble solid particles) that can be simply separated by settling or filtration. |
| Electrodialysis (ED) and Electrodialysis Reversal (EDR) | ED and EDR are considered electro-membrane separation processes as ion-exchange membranes (IEM) that are used to separate different ions present in solution as it permeates owing to electrical potential difference. ED/EDR has been mainly utilized for advanced water deionization, high-efficiency removal of ions in pure and ultrapure water application as well as brackish water desalination. |
| Membrane filtration (MF) | MF is capable of removing not only suspended solid and organic components but also inorganic contaminants such as metal ions. A membrane is a selective layer used to make contact between two homogenous phases with a porous or non-porous structure for the removal of pollutants. Based on the various sizes of the particle, it is divided into three types as below: |
|
Ultrafiltration (UF) | UF utilizes permeable membrane to separate heavy metals with pore sizes in the range of 0.1–0.001 micron which permeates water and low molecular weight solutes, while retaining the macromolecules, particles, and colloids that are larger in size of 5–20 nm. The removal of Cu (II), Zn (II), Ni (II), and Mn (II) from aqueous solutions is achieved by using ultrafiltration assisted with chitosan-enhanced membrane with a rejection of 95–100% or a copolymer of malic acid and acrylic acid attaining a removal efficiency of 98.8% by forming macromolecular structures with the polymers. |
|
Nanofiltration (NF) | NF is a pressure-driven membrane process that lies between ultrafiltration and reverse osmosis. It is able to reject molecular ionic species by making separation of large molecules possible by small pores when they are within the molecular weight range from 300 to 500 Da with a pore diameter of 0.5–1 nm. A current commercial nanofiltration membrane NF270 is used for removing Cd (II), Mn (II), and Pb (II) with an efficiency of 99, 89, and 74%, respectively. |
|
Reverse Osmosis (RO) | In RO, a pressure-driven membrane process, water can pass through the membrane, while the heavy metal is retained. The removal performance of an ultra-low-pressure reverse osmosis membrane (ULPROM) was investigated for the separation of Cu(II) and Ni(II) ions from both synthetic and real plating wastewater. |
| Microfiltration (MF) | MF uses the same principle as ultrafiltration. The major difference between the two processes is that the solutes which are removed by MF are larger than those rejected by UF using the pore size of 0.1–10 μm with applied pressure range of 0.1–3 bar. |
| Photocatalysis | Photocatalysis is based on the reactive properties of electron- hole pairs generated in the semiconductor particles under illumination by light of energy. Metal ions are reduced by capturing the photo-excited conduction band electrons, and water or other organics are oxidized by the balance band holes. Heavy toxic metal ions such as Hg2+ and Ag+, and noble metals can be removed from water by photo deposition on Titania surface-trapped photoelectron states, probably Ti(III), and silver deposition could be observed on the same time scale. |
Figure 1Mechanisms of bacterial biosorbent: (a) on cell surface; (b) within the cell where the HMs are removed.
The promising bacterial strains that can remove HMs via biosorption process.
| Bacterial Biosorbents | Target Metals | Amount of Heavy Metals Uptake (mg/L) | Biosorption | Reference |
|---|---|---|---|---|
| Cr | 200 | 96.6 | [ | |
| Cr | 55.35 | 41 | [ | |
| Cr | 10 | 93 | [ | |
|
| Cr | 164.66 | 82.33 | [ |
|
| Cr | 19.84 | 99.2 | [ |
| Cr | 6.82 | 68.17 | [ | |
| Cr | 96.98 | 96.98 | [ | |
| Cr | 270 | 90 | [ | |
| Pb | 200 | 84.62 | [ | |
| Pb | 300 | 62.28 | [ | |
| Pb | 86.47 | 96.78 | [ | |
| Pb | 400 | >90 | [ | |
|
| Pb | 100 | 97 | [ |
| Pb | 95.04 | 86.25 | [ | |
| Pb | 49.48 | 98.96 | [ | |
| Pb | 60 | 60 | [ | |
|
| Cd | 40.18 | 40.18 | [ |
| Cd | 40 | 80 | [ | |
| Cd | 39.5 | 79 | [ | |
| Cd | 108.2 | 93.76 | [ | |
| Hg | 10 | 99.7 | [ | |
| Hg | 5 | 90 | [ | |
|
| Cd, Pb | 62.8 (Cd); 73.1 (Pb) | 87 (Cd); 98.5 (Pb) | [ |
|
| Pb, Cd | 0.045 (Pb); 0.47 (Cd) | 70.3 (Pb); 76.2 (Cd) | [ |
| Zn | 174 | 100 | [ | |
| Pb, Cu | 20.4 (Cu); 98.25 (Pb) | 25.42 (Cu); 36.07 (Pb) | [ | |
| Pb, Cu, Cd | 990 (Cd); 970 (Cu); 200 (Pb) | >90 (Cd, Cu); 20 (Cd) | [ | |
|
| Pb, Zn | 45 (Pb); 1.08 (Zn) | 97 (Pb); 54 (Zn) | [ |
|
| Cr, Zn | 118 (Zn); 112 (Cr) | 59 (Zn), 56 (Cr) | [ |
| Pb, Cd, Cu | 1.43 (Cu); 0.91 (Pb) 3.66 (Cd) | Pb (83.4); Cu (74.5); Cd (68.4) | [ | |
| Hg, Pb, Cd, Ni | 8500 (Hg); 10,000 (Pb); 1026 (Cd); 8479 (Ni) | 85 (Hg); 97.13 (Pb); 73.33 (Cd) 86.06 (Ni) | [ | |
| Cd, Cu, Pb | 24.64 (Cd); 17.44 (Cu); 19.55 (Pb) | 98.57 (Cd); 69.76 (Cu); 78.23 (Pb) | [ |
The potential bacterial strains that can remove HMs via bioaccumulation process.
| Bacterial Biosorbents | Target Metals | Amount of Heavy Metals Uptake (mg/L) | Bioaccumulation Efficiency (%) | Reference |
|---|---|---|---|---|
| Pb | 2.1 | 98.5 | [ | |
| Pb | 100 | 96 | [ | |
|
| Pb | 100 | 96 | [ |
| Hg | 50 | 91 | [ | |
|
| Hg | 0.25 | 60 | [ |
|
| Cd | 4 | 72.11 | [ |
| Cd | 97.35 | 76.42 | [ | |
| Cd | >90 | >90 | [ | |
|
| Cr | 1500 | 81 | [ |
| Cr | 50 | 82.5 | [ | |
| Cr | 0.46 | 90 | [ | |
|
| Pb, Ni, Cd | 170.7 (Pb); 18.7 (Ni); 25.6 (Cd) | 44.44 (Pb); 16.66 (Ni); 8.3 (Cd) | [ |
|
| Pb, Cd | 2.09 (Pb); 0.37 (Cd) | 98.1 (Pb); 92.5 (Cd) | [ |
| Pb, Cd | 98.2 (Pb); 82.6 (Cd) | >98 (Pb); 75 (Cd) | [ | |
| Zn | 11.76 | 36 | [ | |
|
| Cd, Zn | 220.5 (Cd); 113.5 (Zn) | 98.11 (Cd); 87.33 (Zn) | [ |
| Cr, Zn, Cd | 9.78 (Cr); 14 (Zn); 12.6 (Cd) | 48.93 (Cr); 70 (Zn); 63 (Cd) | [ | |
| Zn, Cd, Pb | 3.83 (Zn); 8.14 (Cd); 4.03 (Pb) | 38.3 (Zn); 81.4 (Cd); 40.3 (Pb) | [ |
Differences between the biosorption and bioaccumulation process of heavy metal removal conducted by bacteria.
| Contents | Biosorption | Bioaccumulation |
|---|---|---|
| General features | Passive process | Active process |
| Ions bound on the surface of ions | Intracellular accumulation of ions | |
| Rapid and simple process | Requires longer time and complex process | |
| Not energy requirement | Requires energy sources for metabolisms | |
| Carried out by both-live and dead biomass | Carried out only by live biomass | |
| No sensitivity to cultivation conditions | Inhibited by the lack of nutrients, low temperature, and metal toxicity | |
| Fresh cultivation medium is not necessary | Need of fresh cultivation medium | |
| Biomass can be regenerated and reuse | Due to the intercellular accumulation, reuse is limited for further purpose | |
| Main affect factors | ||
|
pH and temperature | Can occur in a wide range of pH and temperature | Be sensitive to pH and temperature change led to a significant change in living cells |
|
Selectivity | Can be increased by modification or biomass transformation | Better in the case of biosorption |
|
Concentration and type of pollutant | There is a limitation for maximum biosorption | More significant affect cell growth led to more affect the accumulation ability |
Major advantages and disadvantages of bacterial biosorbent.
| Advantages | Disadvantages |
|---|---|
|
Cost-effective and simple operation owing to utilization of bacterial biomass. Multiple heavy metals uptake at a time. No additional nutrient requirement. Capable of treatment the large volumes of wastewater. Efficient in a wide range of conditions including temperature, pH, salinity, and the presence of various kinds of contaminants. High efficiency by decreasing the volume of solid waste and concentration of pollutants from wastewater. Regeneration of biosorbents. |
Saturation of active sites of metal binding ligands. Incomplete metal removal in real conditions. May need the high energy requirements. Living cells are more efficient than dead cells in removal but: It takes a long time to find the bacterial materials. There are difficulties in controlling and managing bacterial growth and activities. The cost of production and maintenance of living biomass may be high. |
Figure 2Factors affecting the bioremediation process.
Figure 3A schematic diagram representing extremophile candidates tolerant to different harsh environmental conditions that are capable of heavy metal removal.
Figure 4Mechanisms of the resistance of extremophiles.