Treatment of industrial wastewater due to its varied quantitative and qualitative composition is a complex issue, which is still the subject of numerous studies. An example of wastewater whose cleaning up causes many problems are wastewater from dyes, textile, polygraph and mining industry. Industry wastewater is characterized by considerable nuisance and environmental toxicity. First of all, their composition contains dyes and other substances such as: mineral and silicone oils, polycyclic aromatic hydrocarbons, pesticides, detergents, inorganic acids, strong oxidants used as bleaching agents, as well as adhesives and alkali [1]. What is more industrial wastewater has an intense color, a various inhibitors and toxic agents contained in them are poorly biodegradable, sometimes they are characterized by variations in the composition, reaction and pollution load [2]. Due to the diverse nature of mentioned wastewater, various methods (like sorption, coagulation, biodegradation or chemical oxidation) of their treatment, or combining several of them, must be used. Potassium ferrate(VI) has a high value redox potential (2.2 V in acidic solutions), only the fluorine (2.9 V) and the OH hydroxyl radical (2.8 V) have a higher values [3]. Because of this it could be a very effective reagent in various fields including applications in water oxidation catalysis, waste remediation and high capacity battery cathodes production [4]. Moreover it can kill microorganisms, eliminate organic and inorganic contaminants and eliminate suspended/colloidal materials due to its high oxidizing potential and ability to simultaneously generate ferric cations, which can act as a coagulant. Generally the products of decomposed contaminants are water and carbon dioxide and also intermediate products are less toxic than the previous ones. In addition, during the reduction of
One of the most profitable industries in the world are gold mines. The current development of technology, especially computer technology, causes a continuous increase in the demand for this raw material. Gold is an irreplaceable raw material for the production of high–quality conductors, connectors or other technical accessories. The process of gold mining and processing is a complicated operation and one ton of ore gives an average of 6.5 g Au. The extracted rocks are milled to a suitable thickness and an aqueous solution of metal cyanides is added. Under the influence of air oxygen, Au from minerals reacts with CN- ions forming the
After the separation of metallic gold, significant amounts of wastewater are generated, which must be treated [5, 6]. They are characterized by high pH value, high content of heavy metals (among others: Zn, Cd, Cu, Ni, Bi, U), very high content of cyanides, sulfur compounds (sulfides, sulfites), they also contain traces of gold compounds as well as organic compounds. Due to the high toxicity, post-mining wastewater should be cleaned, however, one effective method of treatment has not been developed. To treat these wastewater, methods such as ozonation, chlorination, oxidation with H2O2, sedimentation and biological methods are used [7]. The most important module for the purification of this type of wastewater should be their oxidation, mostly based on the ozonation or chlorination process. Unfortunately, both these processes have major disadvantages: ozonation is a cost-intensive process, whereas chlorination causes secondary pollution of wastewater with chlorine compounds [6]. In order to reduce the costs of wastewater treatment and to obtain at least a partial distribution of pollutants, K2FeO4 was used for this purpose. Under laboratory conditions, K2FeO4 oxidized many compounds present in wastewater from a gold mine. The following are the compounds found in post-mining wastewater, oxidized by K2FeO4 [7]: Hydrogen sulfide
Thiourea
Thioacetamide
Hydrogen cyanide
Zinc-cyanide complex
In the course of the research, the main focus was put on the degradation of zinc-cyanide complex and free cyanides, because they constitute the largest load of pollutants in post-mining wastewater. By selecting the appropriate pH and reaction time, zinc-cyanide complex was completely removed. In addition, the further activity of K2FeO4 on intermediates of cyanide oxidation, at low pH, allowed their complete decomposition to carbon dioxide and nitrites [6]. The rate of oxidation of CN- ions depended largely on the pH of the reaction. The tests showed that the oxidation reaction was the fastest in the range of pH 7.5–8, while with the increase of pH, the reaction rate was reduced. In addition, if the
Inorganic compounds susceptible to decomposition by using K2FeO4
Compound/Ion | Molar mas, g/mol | Literature |
---|---|---|
HCN | 27.03 | Costarramone et al., 2010 [8], Sharma et al., 1998 [10] |
SCN- | 58.08 | Sharma et al., 2002 [11], Gonzalez – Merchan et al., 2016 [12] |
|
216.48 | Yngard et al., 2008 [13], Tiwari & Lee, 2011 [14] |
|
159.91 | Sharma V.K., 2011 [15] |
|
169.45 | Yngard et al., 2007 [16] |
|
162.76 | Yngard et al., 2008 [13], Osathaphan et al., 2014 [17] |
|
167.62 | Tiwari & Lee, 2011 [14], Sharma et al., 2005 [18] |
NH2OH | 33.03 | Sharma V.K., 2011 [15] |
N2H4 | 32.05 | Sharma V.K., 2011 [15] |
H2S | 34.08 | Sharma et al., 1997 [19], Talaickhoazni et al., 2016 [20] |
|
80.06 | Johnson & Bernard, 1992 [21], Read et al., 2001 [22] |
|
112.13 | Johnson & Read, 1996 [23] |
|
192.19 | Read et al., 2005 a,b [24, 25] |
|
256.32 | Read et al., 2005 a,b [24, 25] |
As3+ | 74.92 | Fan et al., 2007 [26], Lee et al., 2003 [27] |
Natural organic matter (NOM) is a large group of organic carbon compounds occurring in the natural environment, both land and water. It is a matter composed of organic compounds from residues of living organisms, such as plants or animals. Organic molecules can also be produced by chemical reactions, with the basic NOM structures formed from cellulose, tannins, cutin and lignin, as well as from proteins, lipids and carbohydrates. Organic matter is very important for the flow of nutrients in the environment and plays an important role in water retention in soil. The same ability of natural organic matter that helps in the retention of water in the soil, however, poses problems for current methods of water treatment. In an aqueous environment, organic matter binds to metal ions and minerals and due to its high reactivity, it can produce by-products that are harmful to the environment and people [28]. Therefore, researchers are trying to find new ways of drinking water treatment, e.g. using K2FeO4 for several reasons [29]: the reaction rate of K2FeO4 and NOM can affect the rate of Fe(III) formation, which can be used as an in-situ coagulant, NOM causes the water color, which affects its aesthetic and health effect, NOM is a precursor to some disinfection by-products that affect health, NOM increases the solubility of metals in water by complexing them.
So far, little research has been done on the degradation of NOM, and those available in the scientific circuit focus on one or two types of substances such as humic acid (HA) or fulvic acid (FA) [30–34]. Research conducted by Qu et al. [30] showed that the use of K2FeO4 to oxidize FA extracted from the bottom sediment of the Chinese water reservoir, allowed for 90% removed of this acid. The applied dose of FA was 2 mg/L, and K2FeO4 6.8 mg/L, at pH 7.1–7.8. Lim and Kim [32], indicate that K2FeO4 easier removes NOM at pH 3 than at pH 7.8 or 11. On the other hand, Gan et al. [34], provide further data on not only NOM removal but also the reduction of by-products. The authors oxidized the natural organic matter (FA and HA) from the Suwannee River in the USA (Dissolved Oxygen Content, DOC 3 mg/L, pH 7) and achieved a 12% and 28% reduction in DOC using 1 mg/L and 20 mg/L K2FeO4 respectively. Most of the previous work concerned only the oxidation of some NOM fractions using K2FeO4 or was not carried out in experimental conditions similar to water treatment conditions. Sun et al. [35], proposed a novel DEET (N,N-diethyl-3-toluamide) oxidation process by the combined use of K2FeO4 and sulfite ions. The obtained test results indicated that sulfites in combination with K2FeO4 can significantly improve the DEET degradation rate. At the beginning, the researchers checked how degradation works with Na2SO3 and K2FeO4 used separately, and then in a combination of both compounds. After 30 min of reaction using only Na2SO3 (dose 400 µM) at pH 8, practically no degradation of DEET was observed (initial and final concentration was 10 µM). A similar situation took place using only K2FeO4(converted to Fe(VI) ions at 100 µM), under the same reaction conditions. The combination of K2FeO4 and Na2SO3 allowed to remove 78% DEET from the solution within 10 seconds. It was also checked how the initial concentration of DEET affects its degradation efficiency. At a constant concentration of Fe(VI) ions (100 µM) and Na2SO3 (400 µM) for DEET<7 µM, almost complete removal of DEET (95%) in 10 s, at pH 8 was achieved. For doses of 7 µM< DEET<30 µM, only a 45% removal, in 10 s, at pH 8 was noted. The effectiveness of DEET degradation in the Fe(VI)/Na2SO3 system was closely related to the doses of both reagents, the initial concentration of DEET and the pH value. It was also shown that the presence of humic acids, chloride, bicarbonate and carbonate ions, clearly inhibited the decomposition of DEET [35].
In the nineteenth century, a lot of methods were developed for obtaining synthetic dyes on a larger scale. Since then, about 10.000 synthetic dyes have been created, often with a complicated chemical structure, which in most cases displaced natural dyes from production [36, 37]. Currently, artificial colors are used in various industries, especially in the textile, pulp and paper, pharmaceutical, cosmetics and food industries. The highest consumption of dyes is recorded in the textile industry. Pigment dyes, which are organic and inorganic substances difficult to biodegradable, may occur in many types of wastewater [38]. These dyes can effectively inhibit photosynthesis and biochemical pathways in the organisms of various plants and animals living in the aquatic environment [39]. In addition, some of the dyes may have toxic, mutagenic, teratogenic or carcinogenic effects on various aquatic organisms [40]. Additionally, the surface waters are a source of water for people. There has been a long-standing interest in ways of degradation of dyes present in industrial wastewater. Various methods of this type of wastewater treatment were developed, including physicochemical methods (adsorption, coagulation, filtration, ion exchange), chemical (ozonation, chlorination), Advanced Oxidation Processes (AOPs) such as photochemical methods (UV-photolysis, photo-Fenton reaction, processes using ultrasounds, UV/H2O2 processes, UV/O3 and others) and chemical methods (Fenton reaction, oxidation by O3 and H2O2, electrochemical oxidation). Although the above methods have been successfully used to eliminate dyes from contaminated water, they have many limitations due to the need to use specific adsorbents, chemical substances (including catalysts), enzymes, as well as specific technological conditions (e.g. high temperature, pressure, UV radiation). Among the AOPs methods used for the degradation of dyes in wastewater, the Fenton reagent (Fe2+/H2O2) and its modifications has been quite often used for some time [41, 42]. The advantage of using the Fenton reagent is the high oxidation potential of the resulting hydroxyl radicals and the fact that the Fenton reaction occurs at ambient temperature and normal pressure. An interesting alternative for using AOPs processes for the degradation of dyes in wastewater, landfill leachate and other types of wastewater is using K2FeO4, due to the very high oxidation potential of Fe(VI) ions and the formation of usually less toxic or non-toxic by-products in relation to the initial impurities [43]. Potassium ferrate(VI) has been used as an oxidizing and coagulating agent for the degradation of methylene blue (MB) present in dye wastewater. The authors [44] used Fourier-transform infrared spectroscopy (FTIR) to study degraded MB molecules after using K2FeO4. The dye concentration was 1 mg/L, the dose of K2FeO4 20–250 mg/L, pH 7–8, and the reaction time 20 min. The obtained results showed that the peaks characteristic for this dye disappeared, which proved that it was completely degraded. In addition, the MB removal efficiency was estimated by measuring the UV–VIS adsorption spectrum with the K2FeO4 solution. The pure MB solution showed maximum absorbance at 664 nm, however, the absorbance measured after the reaction showed no peak in the electron spectrum, suggesting that the dye was completely oxidized. The most favorable dye degradation conditions were also determined: K2FeO4 concentration 70 mg/L, pH 7 and reaction time 20 min. Potassium ferrate(VI) was also used as an oxidizer to remove Orange II dye from an aqueous solution. The effectiveness of the discoloration of the Orange II dye using K2FeO4, KMnO4 and ferrate(VI)-hypochlorite liquid mixture was investigated [45]. Oxidant concentrations were 10 mg/L, dye concentration 50 mg/L, pH 3 and reaction time 10 min. Under these conditions a decolorization efficiency for KMnO4 solution was 17.7%, 62% for K2FeO4 solution and 95.2% for ferrate(VI)-hypochlorite liquid mixture. The obtained results indicate the possibility of rapid destruction of chromophores and aromatic rings in the dye tested, especially in the case of K2FeO4 and ferrate(VI)-hypochlorite liquid mixture. Potassium ferrate(VI) also effectively degraded azo dye (Brilliant Red X–3B). It was shown that the pH value, the initial concentration of the dye and the dose of K2FeO4, had a significant influence on the efficiency of the oxidation process. Under the most favorable conditions, in which the starting dose of the dye in the aqueous solution was 49.2 mg/L, K2FeO4 concentration 25 mg/L, pH 8.4, after 20 min reaction, 99% discoloration was obtained. The disappearance of the color was much faster than the decrease in the COD and TOC values, since after 60 minutes of reaction only 42% reduction of the COD value and 9% decrease of the TOC value were obtained. This was most likely caused by the destruction of chromophores and the formation of various by-products, such as: naphtalene, phthalic acid, 1-isocyanato-phenol, azobenzene, muconic acid and hydroquinone [46]. What is more, Han et al. [47] investigated the effect of anions on the decolorization of X–3B dye by K2FeO4 and KMnO4. It has been shown that the presence of Cl-,
Eutrophication, the increase in the fertility of waters, is caused by the growing pollution of the natural environment with biogenic substances, mainly nitrogen and phosphorus compounds, which are used, among others, in agriculture. Eutrophication causes the excessive development of phytoplankton organisms, which in consequence is associated with the reduction of light transmittance to deeper parts of water reservoirs, overgrowth of hydrotechnical devices and release of various toxins to the aquatic environment by algae. Unfortunately, for many reasons, the causes of water eutrophication can not be completely eliminated, which necessitates the elimination of phytoplankton in water treatment stations. Phytoplankton (algae, cyanobacteria) removal processes in water treatment plants mainly boil down to coagulation, sedimentation and or filtration processes. These processes allow the removal of nearly all phytoplankton, however, remains the problem of the water smell and the presence of toxic compounds (anatoxin-a, anatoxin-a(s), aplysiatoxin, cylindrospermopsin, microcystin LR, nodularin R, saxitoxin), secreted by algae. In order to eliminate these problems, oxidation processes using strong oxidants, e.g. chlorine compounds or ozone are used. The addition of an oxidant also increases the efficiency of the coagulation process itself, and reduces the need for coagulant [49]. The results of research conducted using K2FeO4, as a compound supporting the coagulation process and aimed at the elimination of odor and toxic compounds, indicated the possibility of effective use of this oxidant. During the tests, the water from the water reservoir in which the eutrophication processes took place was treated. The presence of organisms such as
Potassium ferrate(VI) is a very promising oxidizing compound, which is still mainly in the field of laboratory research. K2FeO4 has many unique properties – it is non-toxic and environmentally friendly. As a result of using K2FeO4, products with significantly lower toxicity than toxicity of starting substrates or non-toxic products are usually formed. What is more K2FeO4 can act bi-directionally, i.e. as the oxidant in the first stage and as a coagulant in the second stage of the purification processes. As a result of contact with contaminants, it acts as an oxidizer, on the other hand, when Fe(VI) ions are simultaneously reduced to Fe(III), Fe(OH)3 can be precipitated, and acts as a coagulant. Moreover, potassium ferrate(VI) does not act selectively and can degrade all kinds of pollutants. Literature studies indicate the possibility of using K2FeO4 for the decomposition of many contaminants like: metal cyanides, organic compounds, dyes and algae present in water and wastewater. However, it should be noted that at the current stage of research and experience, the use of K2FeO4 on a larger scale is also related to technical and technological constraints, mainly the complicated and costly process of its production. The wider implementation of K2FeO4 method on a technical scale, as in any case, requires further research on a wider scale and also reduction of production costs. The application of K2FeO4 for removal of another types of pollutants (endocrine disrupting chemicals, surface active agents, personal care products and pharmaceuticals) will be the subject of next review paper.