| Literature DB >> 35340731 |
K Sathya1, K Nagarajan2, G Carlin Geor Malar1, S Rajalakshmi1, P Raja Lakshmi1.
Abstract
In recent years, rapid development in the industrial sector has offered console to the people but at the same time, generates numerous amounts of effluent composed of toxic elements like nitrogen, phosphorus, hydrocarbons, and heavy metals that influences the environment and mankind hazardously. While the technological advancements are made in industrial effluent treatment, there arising stretch in the techniques directing on hybrid system that are effective in resource recovery from effluent in an economical, less time consuming and viable manner. The key objective of this article is to study, propose and deliberate the process and products obtained from different industries and the quantity of effluents produced, and the most advanced and ultra-modern theoretical and scientific improvements in treatment methods to remove those dissolved matter and toxic substances and also the challenges and perspectives in these developments. The findings of this review appraise new eco-friendly technologies, provide intuition into the efficiency in contaminants removal and aids in interpreting degradation mechanism of toxic elements by various treatment assemblages.Entities:
Keywords: Challenges and perspectives; Environmental degradation; Hybrid/integrated system; Industrial growth; Recent developments; Resource recovery
Year: 2022 PMID: 35340731 PMCID: PMC8935115 DOI: 10.1007/s13201-022-01594-7
Source DB: PubMed Journal: Appl Water Sci ISSN: 2190-5495
Fig. 1Statistical data on global industrial growth (Radulescu IG et al. 2021, Christina Majaski. 2020, Svetlana Gusarova. 2019, Rachel S Salzman. 2021) (Standard of Fig. 1 is improved including caption)
Fig. 2Treatment methods of electric power plants effluents
Waste water effluent analyses of the electric power plants (data provided in this table has been updated)
| Parameters | Average | Maximum | Standard sewer | Standard irrigation | References |
|---|---|---|---|---|---|
| Temperature (°C) | 29 | 36 | – | – | Ravindra.D. Kali et al. ( |
| PH | 7.9 | 9.4 | 5.5–9.5 | 6.5–8.4 | Ravindra.D. Kali et al. ( |
| BOD (mg L−1) | 13 | 43 | 800 | – | Ravindra.D. Kali et al. ( |
| COD (mg L−1) | 28 | 64 | 2100 | Prerana kane et al. ( | |
| Zn (mg L−1) | 0.3 | 6.75 | 15 | Prerana kane et al. ( | |
| Cl (mg L−1) | – | 711 | – | 350 | Saha PD et al. ( |
| FOG (mg L−1) | 0.5 | 2.0 | 50 | 5 | Saha PD et al. ( |
BOD biological oxygen demand; COD chemical oxygen demand; FOG fats, oils and grease
Fig. 3Methods in reduction of nuclear liquid effluents
Common radioactive nucleotides
| Category | Commonly reported radionuclides | References |
|---|---|---|
| Fusion and Activation gases | Krypton, Xenon, Argon | Stram et al. ( |
| Halogens | Iodine, Bromine | Harris JT et al. ( |
| Particulates | Cobalt, Cesium, Chromium, Manganese, Niobium | Harris JT et al. ( |
| Mixed fission and activation products | Iron, Cobalt, Cesium, Chromium, Manganese, Zirconium, Niobium, Iodine | Kamdi et al. ( |
| Tritium | Hydrogen | Kamdi et al. ( |
| Dissolved and entrained noble gases | Krypton, Xenon | Stram et al. ( |
Literature on petroleum waste water treatment, parameters and treatments
| Pollutant type | Parameters | Treatment | References |
|---|---|---|---|
| Petroleum refinery effluent | COD, BOD, Oil and Grease | Identified photocatalytic degradation as efficient technique | Henrik Pederson et al. ( |
| Oil and greasy effluent | COD | Significant amount of COD (about 85%) reduction within 10 min | Correia T et al. ( |
| Heavy oil produced as effluent | BOD, COD, TKN, Oil | Surface flow constructed wetland can be removed | Correia T et al. ( |
| Highly saline waste water | NaCl, turbidity | RO is efficient for removing the salt concentration and organic matters | Mishra A et al. ( |
| Oily waste water | COD and oil Content | Photocatalytic decomposition of oily waste water by modification of catalyst activity | Henrik Pederson et al. ( |
Toxic effects caused by various pollutants generated from effluent of iron and steel plant
| Class of pollutants | Toxic effect | Disinfection | Reference |
|---|---|---|---|
| Heavy metals | Poisonous interference to enzyme systems and metabolism of body | Blood and cardiovascular, reproductive and urinary system | Sinha S et al. ( |
| Aromatic compounds | PAH have different type of toxic action, depending on the compound | Non-polar narcosis, photo toxicity results in mutagenicity and Carcinogenicity | CL Beh et al. ( |
| Surfactants | Enhance the bio availability and stimulate the biodegradation | Negative impact on the survival of heterotrophic nanoflagellates and ciliates | Das et al. ( |
| Cyanides | Dynamic effects depend on the dose, route and speed of administration including the physical condition of Recipient | Lethal toxicity after inhalation of hydrogen cyanide gas affects many functions in the body | Abhay et al. ( |
| Fluorides | Intake of 20–40 mg/day can inhibit the important enzyme phosphatase | Osteoporosis and arthritis, cancer, infertility brain damage | Pallabi Das et al. ( |
Fig. 4Various treatment methods in food industry
Parameters in dairy industry effluent (data provided in this table has been updated)
| Parameters | Effluents released | Average | References |
|---|---|---|---|
| PH | 1–5.8 | 6.5–8.0 | Shete BS et al. ( |
| Temp (°C) | 25–50 | 33–38 | Zhang T et al. ( |
| BOD (mg L−1) | 1300 | 100 | Kolhe AS et al. ( |
| COD (mg L−1) | 2400 | 250 | Ahmed T et al. ( |
| TSS (mg L−1) | 700 | 100 | Sinha S et al. ( |
| TDS (mg L−1) | 5600 | 2100 | Tikariha A et al. ( |
| Oil & Grease (mg L−1) | 35 | 10 | Ahmed T et al. ( |
Composition of effluent from paper and pulp industry (Data provided in this table has been updated)
| Process | BOD | TSS | COD | Pt-Cd (kg) | References |
|---|---|---|---|---|---|
| TMP | 13–22 | 50–80 | Gautam et al. ( | ||
| Mechanical | 8.5–14 | 10–30 | 20–55 | Gautam et al. ( | |
| Bisulphite | 10–30 | Sudarshan et al. ( | |||
| Unbleached | 25–50 | 10–110 | 75–150 | Cabrera et al. ( | |
| Bleached | 20–60 | 20–150 | 35–120 | Cabrera et al. ( | |
| Kraft-unbleached | 1–20 | 0.2–15 | 7–50 | 20–50 | Elliot et al. ( |
| Bleached normally | 0.2–40 | 0.2–10 | 4–90 | 100,240 | Elliot et al. ( |
| OZP bleaching | 1–20 | 40–80 | Cadat et al. ( | ||
| CTMP | 17–30 | 60–100 | Forster et al. ( | ||
| Bleached | 20–40 | 10–30 | 80–130 | Forster et al. ( |
Types of pulp and their uses
| Type | Variant | Description | End-use | References |
|---|---|---|---|---|
| Mechanical pulp | Stone Ground wood Pulp | Mechanical grinding of the wood into short fibers | Used in the newsprint and wood containing paper, such as lightweight coated Papers | Devendra singh et al. ( |
| Thermo- mechanical Pulp (TMP) | The wood particles are softened by the steam before entering the pressurized refiner | Mainly used in the super calenderer papers | ||
| Semi-chemical pulp | Semi-Chemical Pulp | Produced in the same way as of TMP, but the wooden particles are made to undergo the chemical treatment before entering the refiner | Used in the tissue manufacture. Some CTMP is also used for writing and printing Grades | Omid Ashrif et al. ( |
| Chemical pulp | Sulphite Pulp | Produced by cooking wood chips in the pressure vessel in the presence of bisulphate liquor | Varies from newsprint, printing and writing Papers | Cadet et al. ( |
| Sulphate/Kraft | Pulp is produced by cooking the chips in the pressure vessel in the presence of sodium hydroxide liquor | Pulp used for the graphic designing papers tissues and carton boards |
Technologies for the recovery of valuable substances from different industrial wastewater
| S.No | Industry sectors | Valuable products recovered | Technical method applicable for recovery | Advantages | Disadvantages | References | |
|---|---|---|---|---|---|---|---|
| Recovery of valuables (metals, solvents) | Recovery of process streams (electrolytes, inorganic acids) | ||||||
| 1 | Electrical power plants | Non-ferrous metals like copper, zinc, tin etc. and | Cr, Zn—electrolytes, | Chemical oxidation, reduction | High reaction rates, provides complete mineralization of organic compounds | Operational problems as other reference electrodes are used | Liu M et al. ( |
| 2 | Nuclear power plants | Uranyl nitrate (for the conversion of uranium to fuel)—using tributyl-phosphate | Boric acid, polyantimonic acid, hydrous titanium oxide (inorganic sorbents used for treatment of radioactive waste streams) | Selective ion exchange | Selective removal of specific radionuclides, low cost, no addition of chemicals | Large pH changes in the production process, time consuming | Ohto H et al. ( |
| 3 | Mining | Gold, silver, copper, nickel, niobium, tantalum, cobalt, zinc, zirconium & other rare earth elements | Glutaric acid (from leaching process), H2SO4 | Extraction and using special adsorbents | Highly effective process with rapid kinetics | Expensive | Mfune O et al. ( |
| 4 | Ceramics | Tantalum, niobium oxide—using liquid membranes | Solvents like xylene present in acrylates, epoxies, etc. | Cementation | Controlled potential permits for the separation of precious metals, effective when carried out by reduction with metallic iron | Excess conciliatory metal consumption | Jouhara H et al. ( |
| 5 | Pharmaceutics | Acetone, hexane, isopropanol | Electrolytes like sodium chloride, calcium gluconate | Chromatography | High accuracy, precision, recovery | Since the eluent is itself an electrolyte, it is difficult to determine the separated analytes against eluent | Savelski MJ et al. ( |
| 6 | Food | Deep eutectic solvents like choline chloride with glycerol, phenyl acetic acid that is used for the separation of organic compounds such as phenolic, aromatic, sugars, flavonoids from food samples | Nitric acid (mineral acid), hydrochloric acid, lactic acid, etc. | Crystallization and evaporation | Low temperature and less energy requirement | Yield is limited by phase equilibrium | Hernández K et al. ( |
| 7 | Machinery | Oils | Acetone, hexane, xylene, methyl ethyl ketones, alcohols | Resin adsorption | High capacity and selectivity of the resin | Excess rinse time and migration of cation resin into anion unit can cause leakage problems | Dutournié P et al. ( |
| 8 | Organic chemicals | Organic solvents like acetone, isopropanol, methanol, methanol, ethanol, hexane | Inorganic acids such as HCl, HNO3, H2SO4 | Acid and ion retardation | High accuracy, recovery and regeneration limits the emission of harmful gases | High energy consumption, lack of selectivity towards heavy metals | Wang S et al. ( |
| 9 | Agriculture | Special metals like lead, chromium, arsenic, zinc, cadmium, copper, nickel, etc. | Sodium sulfate, hydrofluoric acid (applied in the production of insecticide and fertilizer) | Sulfide and organosulfate precipitation | Highly efficient towards heavy metals and feasible | Formation of oligomers | Xu M et al. ( |
| 10 | Battery manufacture | Metals and metal-oxide such as nickel, lithium, cobalt-oxide | Electrolytes like NaCl, KCl | Hydroxide-precipitation | Low cost of execution, simple process, easy pH adjustments | Low solubility of the metal, sensitive to the concentration of precipitating agent | Chanthapon N et al. ( |
| 11 | Petrochemicals | Hexane, ethanol, methanol, acetone and precious metals like platinum, palladium, rhenium (from the spent catalyst) | Hydrochloric acid | Electrochemical recovery | No chemical addition, high efficiency, possibility for energy and resource recovery | Anode inactivation may happen | Santos PG et al. ( |
| 12 | Textile | Heavy metals like Cd, As, Pb, Cu, etc. and chlorinated solvents | Acid, reactive and direct dyes using anion exchange resins | Bulk solids and fabrics filtration, nanofiltration, adsorption | Ease of operation, reliable, low power consumption, high efficiency | Expensive regeneration process | Thamaraiselvan C et al. ( |
| 13 | Metal refinery | Gold, silver, platinum, and other metals like Cd, Mo, Pb, Ni, etc. | Tartaric acid, acetic acid, EDTA | Flotation | Efficient separation, applicable for low grade embedding | Causes environmental pollution, finer grinding particle size is needed | Garole DJ et al. ( |
| 14 | Solar industry (photovoltaics) | Metals like silicon, silver, copper, aluminium, etc. | Hydrohalic acid | Sedimentation and centrifugation | Labor-intensive, short harvesting times | Less flexibility and suitable for larger volumes | Igoud S et al. ( |
| 15 | Iron and steel | Manganese, iron, aluminium, silicon, titanium, vanadium, etc. | Sulphuric acid, butyric acid, and other organic and mineral acids | Flocculation and precipitation | Process simplicity and integrated physicochemical technique | Not cost-effective, system controls are required | Wang LP et al. ( |
| 16 | Semiconductor s | Metalloids such as antimony, selenium, gallium, germanium, etc. | Sodium chloride, poly-ethylene terephthalate (PET) | Electrodialysis | Property of polarity reversal allows to perform in the absence of chemicals | Ion diffusion is non-linear to applied voltage after certain current density | Eng CY et al. ( |
| 17 | Dairy | Heavy metals like lead, chromium and trace elements like zinc, copper, iron | Citric acid, ammonium molybdate, potassium antimony tartarate, lactic acid, etc. | Diffusion dialysis | Uniformity, optimum performance, low neutralization costs | High operational cost and high consumption of water and energy | Brião V. B et al. (2019) |
| 18 | Leather | Synthetic tanning agents such as formaldehyde, glutaraldehyde, phenols, acrylates, etc., sulfonated oils, metals like cerium, manganese, chromium, aluminium | Formic acid, phosphoric acid, nitric acid (which are complexing agents for the removal of chromium from leather scraps) | Distillation and rectification | Energy saving operation, less theoretical stage requirements | High operating costs | China CR et al. ( |
| 19 | Paper and pulp | Carbon, disulfide methanol, acetone, methanol (used for wood-chips digestion, spent liquor evaporation) | Potassium nitrate, nitric acid, sulphuric acid, saccharinic acid, resin acid, formic acid | Activated carbon adsorption | Provides high surface area and significant stability | Product recovery requires special, expensive distillation/ extraction | Elakkiya E et al. ( |
| 20 | Oil extraction | Metal halides like stannous chloride and crude oil | Polyacrylic acid, | Reverse osmosis | Separation of dissolved substances, cost-effective | Possibility of fouling since it is a membrane-based technique | Chang H et al. ( |
Comparison among effluent treatment methods
| S.no | Treatment methods | Illustration | Merits | Demerits | References |
|---|---|---|---|---|---|
| 1 | Membrane filtration | Removal of solids from wastewater based on ultrafiltration/microfiltration | Feasible to attain the required water and discharge concentration factors | Not applicable for shear sensitive materials and expensive | Barakat M.A ( |
| 2 | Activated carbon adsorption | Adsorption of toxic organic compounds from the effluent | Pertinent for the removal of wide variety of dyes like azo, reactive dyes, etc. | Regeneration is expensive and involves adsorbent loss | Barakat M.A ( |
| 3 | Photocatalysis | Advanced oxidation technology for eliminating the determined organic compounds and microbes from wastewater | Low operational costs and absolute mineralization of chemical substances | Fouling of photo- catalysts | Threrujirapapong T et al. ( |
| 4 | Electro-coagulation | Destabilization of suspended, emulsified and dissolved contaminants in the effluent by the application of electric current | No chance of secondary pollution as no chemicals are added | Requires regular replacement of anode | Gatsios E et al. ( |
| 5 | Bio-augmentation | Enzymatic treatment to remove pollutants from the wastewater | Improves contaminant degradation | Rehabilitation result may be incomplete | Bora T et al. ( |
| 6 | Biodegradation | Primary removal mechanism for emerging organic pollutants in wastewater | Simple, economically feasible | Necessary to create an optimally favorable environment | Barakat M.A ( |
| 7 | Nanotechnology | Application of nanoparticles for the removal of contaminants from the effluent | Complete degradation of pollutants | Recovery of nanocatalyst is tedious | Bora T et al. ( |
| 8 | Ozonation | Waste water treatment technique based on the infusion of ozone in water | Increases the dissolved oxygen content in water | Cost of treatment is comparatively high | Cano Quiroz A et al. ( |
Modern methods of treatment of wastewater effluent from different sources
| S.No | Type of industry | Effluent composition | Recent advancements in effluent treatment | Treatment category | Target of removal | Merits | Demerits | References |
|---|---|---|---|---|---|---|---|---|
| 1 | Electric power plants | Methane, siloxanes, carbon-dioxide, ammonia, hydrogen sulphide, suspended solids | Development of microbial fuel cell with biocatalysts for concurrent electricity production and pollutant removal from effluent | Biological | Ammonia, Carbon-dioxide, methane through nitrification, denitrification and bio-mineralization | Offers better aversion to environmental stress | High cost and short life span | Guo Y et al. ( |
| 2 | Battery manufacture | Metals like aluminium, cobalt, copper, lead, iron, hydrogen fluoride, lithium, manganese and nickel | Application of pyro, hydro and biohydro—metallurgy for metal extraction from the effluent | Mechano-chemical | Nickel, lithium, cobalt | Separation of valuable metals and economically viable | Reliant to chemical composition and high energy consumption | Mossali E et al. ( |
| 3 | Nuclear power plants | Gaseous (inert gas, halogen, aerosol) and liquid (tritium) radioactive substances | Solidification with barriers to cease water and prevent the water radio-nuclide migration and droning in intense development secluded with biosphere | Chemical | Radioactive materials | Harmless to ecosystem and human beings | High operational cost | Ye et al. ( |
| 4 | Mines and quarries | Sulphide minerals such as suchlike pyrite (FeS2), pyrrhotite (FeS) | Bioremediation and phytoremediation that relies on microbes to degrade the organic contaminants in the wastewater effluent | Biological | Polymetallic sulphides | Economical and less disruptive to the environment | Sensitive to toxicity level | Agboola O et al. ( |
| 5 | Food | Organic compounds, suspended solids, sugar, fats, color, preservatives and nutrients | Employment of hydrophobic neoteric solvents as extractants such as eutectic solvents, ionic liquids, bio-based solvents etc. for phenolic compound separation from food effluents via liquid–liquid extraction | Physico-chemical | Phenolic compounds (flavonoids and non-flavonoids) | Facilitates the separation of high value-added compounds such as phenolic anti-oxidants | Time consuming process and the solvent should be evaporated to concentrate the extract | Canadas R et al. ( |
| 6 | Agriculture | Antibiotics, synthetic compounds, organic compounds and suspended solids, nitrogen and phosphorus | Incorporation of micro-algae into wastewater effluent based on autotrophic nitrification and heterotrophic denitrification for intensified biological N & P removal | Biological | Nitrogen, phosphorus and other organic waste | Eco-friendly and sustainable alternative to conventional biological treatment | High energy requirement and overall cost | Mohsenpo ur SF et al. ( |
| 7 | Dairy | Lactose, fats, whey proteins, chlorides, sulphate, soluble organics, suspended and dissolved solids, BOD, COD | Implementation of unmodified rice husk (by-product of rice milling) as a biosorbent which gets protonated at low pH and thereby capturing the organic materials to the binding sites | Physico-chemical (adsorption) | Organic substances | Easy accessibility of raw materials and cost-effective | Usage of high adsorbent dosage leads to COD loading | Pathak U et al. ( |
| 8 | Oil extracting mills | Organic carbon, nitrogen, methane, carbon-dioxide, hydrogen sulphide, suspended solids, BOD, COD | Utilization of palm kernel shell for the development of biomass adsorbent through the integration of zeolite and iron oxide for the adsorption of organic pollutants from the effluent | Physico-chemical (adsorption) | Heavy metals, diligent organic/inorganic contaminants | Increased stability and adsorption efficiency, good separation, aids in the conversion of solid waste to useful adsorbent | High pre-production cost | Jun KC et al. ( |
| 9 | Petroleum and petrochemicals | Dissolved oil, hydrocarbons, gases like H2S, CO2 and organic acids | Hybrid system using continuous flow intermittent cleaning biofilm technology -based moving bed biofilm reactor and assimilated native microbial association – based continuous stirred tank bioreactor | Biological | COD and total petroleum hydrocarbons | High resistance to toxic effects, increased mass transfer between hydrocarbon and biocatalyst, highly precise | High operational and maintenance costs | Kuyukina MS et al. ( |
| 10 | Organic chemicals | Crude oil and grease, hydrocarbons, BOD, resins, pesticides, synthetic fibers, organic chemicals (benzene, toluene, phenols, etc.) and heavy metals (chromium, lead, copper etc.) | Integrated treatment involving fixed biofilm bioreactor, two-phase partitioning bioreactor, sequencing batch reactor to remove the toxic pollutants | Physico-chemical, biological | Heavy metals and other inorganic matter | Technologically and economically feasible | Sedimentation is required to prevent clogging, time-consuming | Awaleh MO et al.( |
| 11 | Leather | Volatile organic compounds, heavy metals, COD, BOD, dissolved solids, sulphides, calcium/ammonium salts, chromium, H2S | Employment of waste tea leaves (dropped out from teashops/residence) for heavy metal removal from the tannery effluent, due to its good biosorption ability | Physico-chemical (adsorption) | Heavy metals like chromium, iron, nickel, lead | Effective, inexpensive, copiously obtainable cheap | Release of soluble carbon content and applicable only for heavy metal removal | Nur-E-Alam et al. ( |
| 12 | Paper and pulp | Suspended solids, organic matter, chlorinated resin acids, wood extractives, lignin, cellulose, tannins, diterpene alcohols, BOD, COD | Incorporation of fungal consortium ( | Biological | Lignin, cellulose/hemi-cellulose, BOD, COD | Cost effective, ecofriendly | Complexity in micro-biological mechanism, slow process | Ram C et al. ( |
| 13 | Iron and steel | Oil and grease, phenol, cyanides, ore particles, sulfur compounds and metal ions | Employment of steel slags (containing iron oxide) to remove metallic iron, and steel slag-based induction furnace for chromium removal | Physico-chemical method (adsorption) | Heavy metals | Economically sustainable, reuse of steel waste | Stability problems | Branca TA et al. ( |
| 14 | Pharmaceutics | Dissolved and suspended solids, COD, organic matter such as alcohol, aromatic compounds, acetone, antibiotics, chlorinated hydrocarbons | Molecularly imprinting technology that employs molecularly imprinted polymers to produce affinity membranes for the removal of antibiotics from water | Physico-chemical method (membrane filtration) | Antibiotic-tetracycline | High selectivity, affinity, stability, easier operation | High utilization of template molecules | Gadipelly C et al. ( |
| Nanofiltration which is pressure driven membrane separation process for eliminating the antibiotic concentration from the wastewater effluent | Physico-chemical method (membrane filtration) | Antibiotic-amoxicillin | High operational efficiency | Expensive and high energy consumption | ||||
| 15 | Textile | Dyes and fibers (reactive, vat, azoic), toxic chemicals (acids, alkali, surfactant-dispersing agents), heavy metals (copper, chromium, cadmium, zinc etc.) | Photocatalytic degradation using TiO2 nanoparticles, | Chemical (photocatalysis) | Dyes | Application of nanotechnology in textile effluent treatment is efficient in eliminating and retrieving pollutants | Costly, instability of nanoparticles | Kumar PS et al. ( |
| Carbon-based nanomaterials | Physico-chemical (adsorption of pollutants) | Organic/inorganic contaminants | ||||||
| Nanosorbents | Physico-chemical (adsorption of pollutants) | Metal oxides | ||||||
| Zeolites, carbon nanotubes, | Physico-chemical (adsorption of pollutants) | Heavy metals |