| Literature DB >> 28352564 |
Abstract
Heavy metal contamination has been recognized as a major public health risk, particularly in developing countries and their toxicological manifestations are well known. Conventional remediation strategies are either expensive or they generate toxic by-products, which adversely affect the environment. Therefore, necessity for an environmentally safe strategy motivates interest towards biological techniques. One of such most profoundly driven approach in recent times is biosorption through microbial biomass and their products. Extracellular polymeric substances are such complex blend of high molecular weight microbial (prokaryotic and eukaryotic) biopolymers. They are mainly composed of proteins, polysaccharides, uronic acids, humic substances, lipids etc. One of its essential constituent is the exopolysaccharide (EPS) released out of self defense against harsh conditions of starvation, pH and temperature, hence it displays exemplary physiological, rheological and physio-chemical properties. Its net anionic makeup allows the biopolymer to effectively sequester positively charged heavy metal ions. The polysaccharide has been expounded deeply in this article with reference to its biosynthesis and emphasizes heavy metal sorption abilities of polymer in terms of mechanism of action and remediation. It reports current investigation and strategic advancements in dealing bacterial cells and their EPS in diverse forms - mixed culture EPS, single cell EPS, live, dead or immobilized EPS. A significant scrutiny is also involved highlighting the existing challenges that still lie in the path of commercialization. The article enlightens the potential of EPS to bring about bio-detoxification of heavy metal contaminated terrestrial and aquatic systems in highly sustainable, economic and eco-friendly manner.Entities:
Keywords: Bioremediation; Biosorption; Exopolysaccharide (EPS); Heavy metals
Year: 2016 PMID: 28352564 PMCID: PMC5361134 DOI: 10.1016/j.btre.2016.12.006
Source DB: PubMed Journal: Biotechnol Rep (Amst) ISSN: 2215-017X
Homo and hetero-exopolysaccharides.
| EPS Class | Secreted product | Monomers | Linkage | Example Microorganisms | Reference |
|---|---|---|---|---|---|
| Homopolysaccharide | Dextran | Glucose | α-1,6 | ||
| Mutan | Glucose | α-1,3 | |||
| Alternan | Glucose | α-1,3 and α-1,6 | |||
| Reuteran | Glucose | α-1,4 | |||
| Curdlan | Glucose | β -1,3 and | |||
| Levan(fructans) | Fructose | β -2,6 | |||
| Inulin-type (fructans) | Fructose | β -2,1 osidic bonds | |||
| half row | |||||
| Heteropolysaccharide | Alginate | β − | 1–4 bonds | ||
| Xanthan | Glucose backbone, linked with trisaccharide side chain of glucuronic acid, | 2–5 and 2–4 bonds | |||
| LAB( | Glucose,galactose, rhamnose, fructose | 1–2; 1–3; | |||
| Hyaluronan | Glucuronic acid and N-acetylglucosamine | Alternate β -1.4 and β -1,3 bonds | |||
| Sphingans (Gellan, welan, rhamsan and | Rhamnose, glucose, glucoronic acid | 1–3 and 1–4 bonds | |||
Fig 1Biosynthesis of EPS in gram negative and gram positive bacteria, beginning with substrate diffusion, multiple array of enzymatic actions and substrate conversion within intracellular environment, eventual assembly of polysaccharide and export to external surface.
Fig. 2Brief picture of metal microbial interactions taking place through two major mechanisms: Active and Passive. Bioaccumulation, Bioleaching, Biosorption and Redox mediated transformations are the major modes by which microbial cell interacts with and uptakes the heavy metal ion.
Major Advantages and Disadvantages of Pure and Cell bound EPS mediated heavy metal adsorption.
| SN. | ADVANTAGES | DISADVANTAGES |
|---|---|---|
| 1. | Environmentally safe and cost effective adsorbent | Low efficiency of biosorption in real industrial samples |
| 2. | No generation of toxic byproducts | Absence of metal ion selectivity or specificity |
| 3. | Both live and dead cell bound EPS can be used for metal adsorption, dead cells are devoid of hazards posed by living cells | Adsorption is extremely sensitive to physiochemical operation parameters like pH, temperature, ionic strength, presence of other biological ligands which makes real sample application difficult. |
| 4. | Requires milder operating conditions compared to conventional physiochemical methods | Maintaining the viability of live cells at higher metal or toxicant concentration, is challenging |
| 5. | Sensitive and can carry out sequestration even at lower metal ion concentrations | Reusability requires use of weak desorption chemicals which alternatively result in reduced desorption efficiency |
| 6. | Can be recycled after desorption of adsorbed metal ions and the metal ions recovered can be further exploited | A maximum consecutive reusability is limited to 5–10 cycles of sorption-desorption |
Remediation strategies and efficiencies.
| Remediation Strategy | Consortial Source and Specifics | Bacterial species | Heavy Metals Adsorbed | Remediation Efficiency | Reference |
|---|---|---|---|---|---|
| HOMOGENOUS CONSORTIAL EPS | Copper,Lead | 21% Cu2+,18% Pb2+ removal from 0.04 ppm initial metal load | |||
| Arsenic | Upto 5 mmol/L metal ion uptake | ||||
| Activated sludge isolates | Copper | N.A | |||
| Marine bacteria | Cadmium,Copper, Chromium | 65% Cd2+,20% Cu2+; 75% Cr6+ reduction from 100 ppm initial metal load | |||
| Cadmium | 80% Cd2+ removal | ||||
| Cyanobacteria | Manganese | 8.52 mg Mn2+/g EPS | |||
| Lead | 82.22 ± 4.82 mg Pb2+/g CPS | ||||
| Lead | 65 mg Pb2+/g CPS | ||||
| Copper | 115 mg Cu2+/g EPS at 12.3 ppm initial metal load | ||||
| Copper | 85.0 ± 3.2 mg Cu2+/g EPS at 12.3 ppm initial metal load | ||||
| Chromium | 36 mg Cr6+/g EPS at 20 ppm initial metal load | ||||
| Chromium | 90.05 mg Cr6+/g EPS | ||||
| Chromium | 157 mg/g of EPS | ||||
| Cadmium | 80% Cd2+ at 10 ppm initial | ||||
| Cadmium | 80% Cd2+ at 10 ppm initial | ||||
| Soil isolates | Lead, Copper, Zinc | 1103 mg Pb2+/g EPS (98.3%,), | |||
| Lead,Mercury | 40.48% Pb2+(33.5 mg Pb2+/g of EPS); | ||||
| Lead, Nickel, Zinc | 89% Pb2+, 85% Ni2+, | ||||
| GRAS status | Lead, Cadmium | 200–300 mg Pb2+/g EPS, | |||
| Copper | 1602 mg Cu2+/g EPS | ||||
| Lead | 276.44 mg Pb2+/g EPS, at 1000 ppm initial metal load | ||||
| HETEROGENUS CONSORTIAL EPS | Activated sludge mixed consortia | Zinc, Copper, Chromium Cadmium | 85 to 95% reduction from initial metal load of 10–100 ppm | ||
| Lead Cadmium | N.A | ||||
| Gram negative microbial consortia | Zinc, lead, Chromium, Nickel, Copper, | 75 to 78% reduction in metal load | |||
| Hydrocarbon contaminated water microbial consortium | Zinc, Copper, Cadmium | 87.12% Cd2+; 19.82% of Zn2+; 37.64% of Cu2+ reduction from 1 ppm initial metal load | |||
| DEAD BIOMASS EPS | Activated sludge isolate | Chromium, Cadmium, Copper | 57.8 mg Cr6+/g EPS at initial metal load of 280 ppm, | ||
| Chromium | 89.87% reduction from initial metal load of 50 ppm | ||||
| Chromium | 89.23% reduction from initial metal load of 50 ppm | ||||
| Chromium | 85.5% reduction from initial metal load of 50 ppm | ||||
| IMMOBILIZED EPS | Alginate bead immobilized | Cadmium, Cobalt, | 64.10 mg Cd2+/g EPS | ||
| Agar Beads immobilized | Lead | 111.11 mg Pb2+/g EPS | |||
| MODIFIED EPS | Phosphorylated bacterial EPS (cellulose) | Lead, Copper, Manganese, Zinc, Cobalt | 90% reduction from initial metal load of 0.1 mmol/dm3 | ||
Patents in the field of microbial EPS involved in heavy metal remediation.
| EPS producing microorganism | Important Experimental Parameters | Metal ion removed | Remarks | Patent No. | Reference |
|---|---|---|---|---|---|
| Hyphomonas MHS-3, Hyphomonas sp. | Adsorbent system was effective over wide range of pH and temperature range of 1–11 and 0 °C –200 °C respectively | Cu2+,Hg2+, Pb2+,Cd2+,Zn2+ | The marine strains were able to remove the metal ions from an initial concentration of 50–100 ppb to US EPA | WO1998030503 A1 | |
| Identification and mixing of genes responsible for polysaccharide synthesis from wild strains for | N.A. | New modified bacterial strains were designed from wild type producing a novel (EPS) with several desirable characteristics that were absent from the parent strain including metal ion chelation | US4948733 A | ||
| Immobilized on water permeable biodegradable, nontoxic support system stable within −15 °C to +65 °C temperature range | N.A | A novel filter devise was designed as a replacement to slow sand filters for the water treatment to render it potable | US5264129 A | ||
| Supported on faujasite (FAU) Zeolite | Cr6+ Removal | Devised for industrial applications for hexavalent chromium removal, through the retention of metal ions in the biofilms, in solutions with concentrations between 50 and 250 mg/L | EP1912905 A1 | ||
EPA–Environment protection agency.