Relevant bibliographies by topics / Industrial wastewater

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Industrial wastewater'

Author: Grafiati
Published: 4 June 2021
Last updated: 9 March 2023

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Journal articles on the topic "Industrial wastewater"

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Gulyas, H., R. von Bismarck, and L. Hemmerling. "Treatment of industrial wastewaters with ozone/hydrogen peroxide." Water Science and Technology 32, no. 7 (October 1, 1995): 127–34. http://dx.doi.org/10.2166/wst.1995.0217.

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Treatment with ozone and ozone/hydrogen peroxide was tested in a laboratory scale reactor for removal of organics from four different industrial wastewaters: wastewaters of a paper-mill and of a biotechnical pharmaceutical process as well as two process waters from soil remediation by supercritical water extraction. Moreover, an aqueous solution of triethyleneglycoldimethylether and humic acid which was a model for a biologically treated oil reclaiming wastewater was also oxidized. The aim of the oxidation of the pharmaceutical wastewater was the removal of the preservative 1.1.1-trichloro-2-methyl-2-propanol (TCMP). Although TCMP could easily be removed from pure aqueous solutions by treatment with ozone/hydrogen peroxide, the oxidation of the wastewater failed to be effective in TCMP degradation because of competitive ozonation of other organic solutes in the wastewater. The ozonation of the paper-mill wastewater and of the soil remediation process waters decreased COD and TOC to some extent. The presence of organic wastewater solutes which contain C-C double bonds (ligninsulfonic acid in the treated paper-mill effluent and humic acid in the oil reclaiming model wastewater) were shown to yield hydrogen peroxide by the reaction with ozone. Therefore, these wastewaters are efficiently ozonated even without addition of hydrogen peroxide. Chemical Oxidation of paper-mill wastewater and of wastewaters resulting from soil remediation did not improve biological degradability of organic wastewater constituents.
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Vítězová, Monika, Anna Kohoutová, Tomáš Vítěz, Nikola Hanišáková, and Ivan Kushkevych. "Methanogenic Microorganisms in Industrial Wastewater Anaerobic Treatment." Processes 8, no. 12 (November 26, 2020): 1546. http://dx.doi.org/10.3390/pr8121546.

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Over the past decades, anaerobic biotechnology is commonly used for treating high-strength wastewaters from different industries. This biotechnology depends on interactions and co-operation between microorganisms in the anaerobic environment where many pollutants’ transformation to energy-rich biogas occurs. Properties of wastewater vary across industries and significantly affect microbiome composition in the anaerobic reactor. Methanogenic archaea play a crucial role during anaerobic wastewater treatment. The most abundant acetoclastic methanogens in the anaerobic reactors for industrial wastewater treatment are Methanosarcina sp. and Methanotrix sp. Hydrogenotrophic representatives of methanogens presented in the anaerobic reactors are characterized by a wide species diversity. Methanoculleus sp., Methanobacterium sp. and Methanospirillum sp. prevailed in this group. This work summarizes the relation of industrial wastewater composition and methanogen microbial communities present in different reactors treating these wastewaters.
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Gao, Ai Hua, Shui Jiao Yang, Shang Bin Hu, Xiao Qing He, and Zhi Guo Lu. "Discharge Plasma for the Treatment of Industrial Wastewater." Applied Mechanics and Materials 71-78 (July 2011): 3075–78. http://dx.doi.org/10.4028/www.scientific.net/amm.71-78.3075.

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The treatment of industrial wastewaters collected from petrochemical works, gypsum plant, and printing and dyeing mill, was investigated at atmospheric pressure in air discharge plasma. The degradation effects of organic contaminants in water were compared for the printing and dyeing wastewater under different discharging conditions and for the wastewater from the other two plants under the same discharging conditions. The influences of several factors on chemical oxygen demand (COD) remove rate were studied experimentally. The results showed that the treatment effects for the same industrial wastewater differed significant under different discharge conditions. There may be a suitable discharge plasma treatment to specific industrial wastewater. Due to the removal rates of COD of industrial wastewaters with discharge plasma isn’t very high, therefore the discharge plasma water treating needs to combine conventional water treating methods or addition other catalyst to effectively remove organic pollutants in wastewater and obtain the expected treatment effect.
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Ahmed, Mohd Elmuntasir, Adel Al-Haddad, and Suad Al-Dufaileej. "Characterization and Profiling of Industrial Wastewater Toxicity in Kuwait." International Journal of Environmental Science and Development 13, no. 2 (2022): 35–41. http://dx.doi.org/10.18178/ijesd.2022.13.2.1369.

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Toxicity reduction is a main criterion in prioritizing industrial wastewater treatment objectives. This paper utilized a comprehensive survey of 41 industrial facilities to characterize their wastewater quality parameters and to assess their wastewater toxicity. The 41 factories were grouped under eleven industrial categories. Microtox relative toxicity test results indicated that industrial wastewater in Kuwait are mostly very toxic to toxic with the exception of farms wastewater which was found to be slightly toxic. The highest ranking toxic wastewaters where found to be metal forming, printing, dairy, slaughterhouses, petrochemical, poultry, food, paper and packaging, beverage, and construction materials industries in order. Among the contributing factors to the toxicity of industrial wastewater are temperature, pH, metals, COD, TOC, NH3, TPH, phenol, and BTEX.
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Prokkola, Hanna, Anne Heponiemi, Janne Pesonen, Toivo Kuokkanen, and Ulla Lassi. "Reliability of Biodegradation Measurements for Inhibitive Industrial Wastewaters." ChemEngineering 6, no. 1 (February 3, 2022): 15. http://dx.doi.org/10.3390/chemengineering6010015.

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Industrial wastewaters may contain toxic or highly inhibitive compounds, which makes the measurement of biological oxygen demand (BOD) challenging. Due to the high concentration of organic compounds within them, industrial wastewater samples must be diluted to perform BOD measurements. This study focused on determining the reliability of wastewater BOD measurement using two different types of industrial wastewater, namely pharmaceutical wastewater containing a total organic carbon (TOC) value of 34,000 mg(C)/L and industrial paper manufacturing wastewater containing a corresponding TOC value of 30 mg(C)/L. Both manometric respirometry and the closed-bottle method were used in the study, and the results were compared. It was found that the dilution wastewaters containing inhibitive compounds affected BOD values, which increased due to the decreased inhibiting effect of wastewater pollutants. Therefore, the correct BOD for effluents should be measured from undiluted samples, while the diluted value is appropriate for determining the maximum value for biodegradable organic material in the effluent. The accuracy of the results from the blank samples was also examined, and it was found that the readings of these were different to those from the samples. Therefore, the blank value that must be subtracted may differ depending on the sample.
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Sreesai, Siranee, and Suthipong Sthiannopkao. "Utilization of zeolite industrial wastewater for removal of copper and zinc from copper-brass pipe industrial wastewaterA paper submitted to the Journal of Environmental Engineering and Science." Canadian Journal of Civil Engineering 36, no. 4 (April 2009): 709–19. http://dx.doi.org/10.1139/l09-008.

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Utilization of zeolite industrial wastewater as a sorbent and (or) precipitant to remove Cu and Zn from copper-brass pipe industrial wastewater was conducted. These wastewaters were sampled and values for pH, temperature, biochemical oxygen demand (BOD5), chemical oxygen demand (COD), total solids (TS), total dissolved solids (TDS), total suspended solids (TSS), and heavy metals were determined. In addition, the sorption isotherms of Cu and Zn in copper-brass pipe industrial wastewater onto solids of zeolite industrial wastewater at various dilutions of copper-brass pipe industrial wastewater were explored. The relationship between Cu and Zn concentrations and their removal efficiencies under different conditions of wastewater pH, contact times, and ratios between copper-brass pipe industrial wastewater and zeolite industrial wastewater was examined. Zeolite industrial wastewater contained various carbonate compounds that contributed to high pH and TDS values, and low heavy metals contamination whereas copper-brass pipe industrial wastewater had a low pH value and was contaminated with heavy metals, especially Cu and Zn. Application of zeolite industrial wastewater significantly increased the pH of copper-brass pipe industrial wastewater and consequently removed Cu and Zn. The increase in pH of the wastewater mixture significantly enhanced the heavy metals removal. The Langmuir equation described sorption isotherms of Cu and Zn onto solids of zeolite industrial wastewater at neutral pH (6–7) while the Freundlich equation fitted well at pH > 12. The maximum Cu (97%–98%) and Zn (92%–96%) removal efficiencies occurred at the original pH 12.8 of zeolite industrial wastewater, at the ratio of copper-brass pipe industrial wastewater to zeolite industrial wastewater 3:1 (vol.:vol.) and at 30 min contact time.
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Gulyas, H. "Processes for the removal of recalcitrant organics from industrial wastewaters." Water Science and Technology 36, no. 2-3 (July 1, 1997): 9–16. http://dx.doi.org/10.2166/wst.1997.0471.

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Processes that are suitable for the elimination of recalcitrant organics from industrial wastewaters are reviewed. Most advantageous are separation processes which enable not only reuse of the water phase but also the recycling of the wastewater constituents. Besides separation processes many degradative wastewater techniques are available. However, for the removal of recalcitrant organics biological processes (which are economically beneficial) cannot be chosen, but a variety of nonbiological degradative processes exist which can be divided into oxidative and reductive technologies. The latter are in the research and development state. The chemical oxidative treatment technologies comprise wastewater incineration and wet air oxidation for wastewaters with high organic concentrations, the so-called advanced oxidation processes (AOPs) as e.g. ozone/hydrogen peroxide which generate the nonselective but very powerful oxidant OH radical, and processes with other oxidants as e.g. Fe(VI) compounds or peroxodisulfate. Also electrochemical oxidation of organic wastewater constituents is possible. All degradative processes that do not lead to total mineralization of organic wastewater constituents may form transformation products which sometimes are more toxic than the original organic compounds.
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Böhm, B. "A test method to determine inhibition of nitrification by industrial wastewaters." Water Science and Technology 30, no. 6 (September 1, 1994): 169–72. http://dx.doi.org/10.2166/wst.1994.0265.

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A biotest to investigate wastewaters for the presence of nitrification-inhibiting substances has been developed. The principal feature of the test system is a packed-bed fixed-film biological reactor operated as a differential reactor. The test has been used to determine the effects on nitrification of wastewaters especially from textile and leather industries. Inhibition could be found even when the wastewater was diluted considerably. Tannery sewage may cause particularly severe problems in biological wastewater treatment, as the degree of inhibition of this wastewater has been observed to be similar to that of a solution of 2 mg/L allythiourea.
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Liu, J., and M. Tang. "Wastewater management approach in an industrial park." Water Science and Technology 2017, no. 2 (April 9, 2018): 546–51. http://dx.doi.org/10.2166/wst.2018.160.

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Abstract Many industrial parks adopt a two-tier wastewater management framework whereby tenants and the park are required to build satellite and centralized wastewater treatment facilities, respectively. Due to the diversity of industrial wastewaters, the treatment process scheme in the public centralized wastewater treatment plant (WWTP) may not suit the characteristics of all effluents discharged from the tenants. In consideration of varying wastewater biodegradability, the treatment scheme in a centralized WWTP is advised to install two series of treatment processes. In detail, various effluents from the tenants shall be commingled according to their levels of biodegradability. For the non-biodegradable streams, advanced oxidation processes shall be applied in addition to biological treatments. To facilitate the grouping of effluents, each effluent will be evaluated for its biodegradability. An analytical protocol derived from OECD standard (TG302B) was developed and found effective for biodegradability assessment. A case study is described in this paper to showcase the methodology.
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Zheng, Lina, Qi Liu, Jiajing Liu, Jingni Xiao, and Guangjing Xu. "Pollution Control of Industrial Mariculture Wastewater: A Mini-Review." Water 14, no. 9 (April 26, 2022): 1390. http://dx.doi.org/10.3390/w14091390.

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With the rapid development of intensive mariculture, lots of mariculture wastewaters containing residual feed and excrements are discharged into marinelands, leading to coastal pollution. Recently, the environmental problems caused by the discharge of mariculture wastewater have been paid much attention, as have other breeding industries in China. In fact, organic solid waste accounts for most of the pollutants and can be reduced by precipitation or filtration technologies, after which the supernatant can be easily treated by ecological methods. Some national guidelines and relevant local standards have been issued to strictly control the mariculture wastewater, but there are still few effective technologies for mariculture wastewater treatment due to its high salinity and extremely low pollutant concentration. This paper aims to propose feasible pollution control methods of mariculture wastewater according to the wastewater characteristics from different mariculture modes. For raw ammonia-based wastewater, it should be sequentially treated by precipitation, nitrification and denitrification and ecological methods, which would target solid waste, organic carbon/nitrogen and phosphorus removal, respectively. For the nitrate-based wastewater, this just needs denitrification filters and ecological methods for nitrate and phosphorus removal. After an overview of pollution control strategies for different types and scales of industrial mariculture wastewater treatment, some challenges are also mentioned.
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Dissertations / Theses on the topic "Industrial wastewater"

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Kapadi, Shourie. "Biological denitrification system for industrial wastewater." [Gainesville, Fla.] : University of Florida, 2009. http://purl.fcla.edu/fcla/etd/UFE0024688.

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Walker, Gavin Michael. "Industrial wastewater treatment using biological activated carbon." Thesis, Queen's University Belfast, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.295433.

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Zakaria, Khalid. "Industrial wastewater treatment using electrochemically generated ozone." Thesis, University of Newcastle upon Tyne, 2014. http://hdl.handle.net/10443/2596.

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The remediation of industrial wastewater is highly challenging, difficult task, and demands highly efficient technologies. Electrochemical and ozonation technologies are among the most efficient methods in treating the industrial wastewater. The electrochemical generation of ozone can provide very high concentrations of the reagent in both the gas phase and solution. The aim of the research reported in this thesis was to develop durable and highly efficient Ni/Sb – SnO2 anodes to generate ozone and to investigate their efficiency in treating industrial wastewater. Different anode sizes were studied: 0.64 cm2, 6.25 cm2 and 24 cm2 using Ti mesh as substrate. With respect to the 0.64 cm2 anodes, replacing Sb and Ni chlorides with their respective oxides and adding Au or Pb had little or no effect upon the anodes electrochemical properties. The research showed that all 0.64 cm2 anodes were porous with dimensionalities < 2. However, the presence of the Au in the precursors reduced the ozone current efficiency. The 0.64 cm2 anodes achieved ozone current efficiencies of ca. 30% at cell voltages of 2.7 V routinely. Using 6.25 cm2 anodes prepared with the Sb and Ni oxides in the precursor solution and annealed at 550 oC gave electrodes which were durable for more than 200 h operation at a current density of 100 mA cm-2 (corresponding to cell voltages of ca. 3 V) in 1 M HClO4. These current densities and service life are the highest reported for Ni/Sb – SnO2 anodes. A service life of more than 600 h was achieved in a later investigation. The 6.25 cm2 anodes achieved current efficiencies up to 38%, with 25 -30% routinely achievable. The presence of Ni is crucial for ozone generation with optimum Ni content (in the precursor solution) of ca. 1.04 at % Ni. The optimum annealing temperature was 460 oC. In terms of the 24 cm2 anodes, they were employed to prepare membrane electrode assemblies (MEA’s) for ozone generation from deionised (Millipore) water. MEA’s with air breathing cathodes suffered from flooding of the cathode pores, resulting in limited current densities. MEA’s with hydrogen – evolving cathodes did not suffer from flooding or low current densities. Overall, current efficiency of ca. 36 % at cell voltage of 1.6 V (40 mA cm-2) with Millipore water as anolyte was obtained using MEA’s with air breathing Preface vii cathodes; corresponding to a power consumption of 16.7 kWh (kg O3)-1 which is the lowest reported for electrochemical ozone generation of any description, MEA’s with H2 cathodes achieved a current efficiency of 33% at ca. 25 mA cm-2 and a cell voltage of 2.5 V, corresponding to ca. 25 kWh (kg O3)-1. The 0.64 cm2 anodes were used to decolourise solutions containing : Reactive Blue 50 (RB50), Naphthol Green B (NGB) and Congo Red (CR) dyes. The operational conditions of the decolourisation process were investigated and the optimum conditions were: 3 g dm-3 Na2CO3 as electrolyte, 50 mA cm-2 and 200 mg dm-3 dye in Millipore water. RB50 solutions could be decolourised completely within 20 min, with 90% of the COD removal after 60 min, NGB and CR proved more refractory. Indirect oxidation mediated by OH radicals was the main decolourisation mechanism at the Ni/Sb – SnO2 anodes. Ozonation, UV254 irradiation and O3/UV were used to decolourise the dye solutions for comparison with electrochemical decolourisation at the Ni/Sb – SnO2 anodes. Ozone was generated by MEA – based electrochemical cells and ozonation occurred in a bubble column reactor (BCR). The O3/UV combination was the most efficient, achieving 100 % decolourisation of RB50 and NGB solutions within 20 and 35 min, respectively, with 33% and 64% COD removal after 60 min.
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Dragoo, Ron. "Pretreatment Optimization of Fiberglass Manufacturing Industrial Wastewater." Thesis, University of North Texas, 1998. https://digital.library.unt.edu/ark:/67531/metadc277875/.

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Wastewater effluent produced in the fiberglass manufacturing industry contains a significant amount of total suspended solids. Environmental regulations require pretreatment of effluent before it is discharged to the municipal wastewater treatment plant. Chemical precipitation by coagulation and flocculation is the method of pretreatment used at the Vetrotex CertainTeed Corporation (VCT). A treatability study was conducted to determine conditions at which the VCT Wastewater Pretreatment Plant could operate to consistently achieve a total suspended solids concentration ≤ 200-mg/L. Jar tests varied pH, polymer dosage, and ferric sulfate dosage. Total suspended solids and turbidity were measured to evaluate treatment performance. The data were used to determine an optimum set of conditions under project guidelines. Of twelve polymers screened, BPL 594 was selected as the most effective polymer. For cost efficiency in the wastewater pretreatment operation, recommendations suggested that treatment chemical injection be electronically controlled according to turbidity of the treated effluent.
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Tuan, Tong Anh Sittipong Dilokwanich. "Industrial wastewater management of Nhue river, Vietnam /." Abstract, 2006. http://mulinet3.li.mahidol.ac.th/thesis/2549/cd387/4737900.pdf.

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Senior, Kerry Charles. "Biotreatment of industrial effluents containing naphthalene sulphonate." Thesis, University of Kent, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.270819.

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Perera, Kuruppu Arachchige Kalyani, University of Western Sydney, of Science Technology and Environment College, and of Science Food and Horticulture School. "Characteristics of a developing biofilm in a petrochemical wastewater treatment plant." THESIS_CSTE_SFH_Perera_K.xml, 2003. http://handle.uws.edu.au:8081/1959.7/777.

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A study was undertaken to investigate developing biofilms in a petrochemical wastewater treatment plant encompassing the architecture, microflora and the chemical nature of the matrix. Biofilms were developed on glass slides immersed in the activated sludge unit and analysed at known time intervals using a range of techniques. Initially, biofilms were investigated using conventional and emerging microscopic approaches to select a suitable technique. Scanning Confocal Laser Microscopy (SCLM) allowed visualisation of biofilms in situ with minimal background interference and non-destructive and optical sectioning which were amenable to quantitative computer-enhanced microscopy. SCLM was superior over Light microscopy and Scanning Electron Microscopy. This study demonstrated biofilm growth, presence of extracellular polymer substances (EPS) in early biofilms associated with cells and the development of porous nature of mature biofilms including channel-like structures. Overall new information has been obtained on developing biofilms in an Australian petrochemical wastewater treatment plant
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Nazir, Karnachi Nayeem A. "Control of the chemical quality of industrial wastewater." Thesis, Leeds Beckett University, 2008. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.500766.

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Quality control of wastewater is an important treatment process more so now, tnan ever before. Due to an extremely unpredictable nature of the wastewater, which is a mixture of both inorganic and organic waste, it is very difficult to neutralise. Two approaches have been proposed in developing alternative control strategies as suggestions for the pH control of the wastewater in an industrial plant. The first is to develop a mathematical model of a continuously stirred tank reactor (CSTR) with a possible use of MATLAB®. Three different control methods (linear, nonlinear and adaptive) are subject to vigorous theoretical testing and are proposed as a possible solution. The second, a parallel approach, has been to build a laboratory scale experimental reactor using a seven litre continuously stirred tank with monitors for influent flow, influent pH and reactor tank pH. Results suggest that a more sophisticated controller than the simple PID control, currently in operation, could lend Itself to overcoming the problem of persistent large spikes in the pH of the influent. Further work would consider the implementation of these results to the actual industrial wastewater treatment plant.
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Hanna, J. A. "Industrial wastewater treatment using dolomite and dolomitic sorbents." Thesis, Queen's University Belfast, 2006. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.431602.

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Jagadevan, Sheeja. "Hybrid technologies for remediation of recalcitrant industrial wastewater." Thesis, University of Oxford, 2011. http://ora.ox.ac.uk/objects/uuid:295c8a29-42aa-47ee-b2b2-89403cee1886.

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In metal machining processes, the regulation of heat generation and lubrication at the contact point are achieved by application of a fluid referred to as metalworking fluid (MWF). This has the combined features of the cooling properties of water and lubricity of oil. MWFs inevitably become operationally exhausted with age and intensive use, which leads to compromised properties, thereby necessitating their safe disposal. Disposal of this waste through a biological route is an increasingly attractive option, since it is effective with relatively low energy demands when compared to current physical and chemical options. However, biological treatment is challenging since MWF are chemically complex, including the addition of toxic biocides which are added specifically to retard microbial deterioration whilst the fluids are operational. This makes bacterial treatment exceptionally challenging and has stimulated the search and need to assess technologies which complement biological treatment. In this study the remediation, specifically of the recalcitrant component of a semi-synthetic MWF, employing a novel hybrid treatment approach consisting of both bacteriological and chemical treatment, was investigated. Three chemical pre-treatment methods (Fenton’s oxidation, nano-zerovalent iron (nZVI) oxidation and ozonation) of the recalcitrant components followed by bacterial degradation were examined. The synergistic interaction of Fenton’s-biological oxidation and nZVI-biodegradation led to an overall COD reduction of 92% and 95.5% respectively, whereas pre-treatment with ozone reduced the total pollution load by 70% after a post-biological step. An enhancement in biodegradability was observed after each of the chemical treatments, thus facilitating the overall treatment process. The findings from this study established that the use of non-pathogenic microorganisms to remediate organic materials present in MWF wastewater is a favourable alternative to energy demanding physical and chemical treatment options. However, optimal performance of this biological process may require chemical enhancement, particularly for those components that are resistant to biological transformation.
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Books on the topic "Industrial wastewater"

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Agency, Ireland Environmental Protection. Wastewater treatment manuals: Characterisation of industrial wastewaters. Wexford: Environmental Protection Agency, 1998.

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1940-, Patterson James William, ed. Industrial wastewater treatment technology. 2nd ed. Boston: Butterworth, 1985.

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M, Boddu Veera, Peyton Gary R, United States. Army. Corps of Engineers., and Construction Engineering Research Laboratories (U.S.), eds. Advanced oxidation treatment of army industrial wastewaters: Propellant wastewater. Champaign, IL: U.S. Army Construction Engineering Research Laboratory, 1997.

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Shah, Maulin P., ed. Biological Treatment of Industrial Wastewater. Cambridge: Royal Society of Chemistry, 2021. http://dx.doi.org/10.1039/9781839165399.

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Edwards, Joseph D. Industrial wastewater treatment: A guidebook. Boca Raton: Lewis Publishers, 1995.

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1950-, Blackburn James W., ed. The industrial wastewater systems handbook. Boca Raton, FL: CRC Press, 1998.

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Moussa, Moustafa Samir. Nitrification in saline industrial wastewater. Lisse: Balkema, 2004.

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L, Musterman John, ed. Activated sludge treatment of industrial wastewater. Lancaster, Penn: Technomic Pub. Co., 1995.

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Alexandros, Stefanakis, ed. Constructed Wetlands for Industrial Wastewater Treatment. Chichester, UK: John Wiley & Sons, Ltd, 2018. http://dx.doi.org/10.1002/9781119268376.

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Türkman, Ayşen, and Orhan Uslu, eds. New Developments in Industrial Wastewater Treatment. Dordrecht: Springer Netherlands, 1991. http://dx.doi.org/10.1007/978-94-011-3272-5.

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Book chapters on the topic "Industrial wastewater"

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Pintér, János D. "Industrial Wastewater Management." In Nonconvex Optimization and Its Applications, 361–82. Boston, MA: Springer US, 1996. http://dx.doi.org/10.1007/978-1-4757-2502-5_25.

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Moore, James W. "Industrial Wastewater Management." In Balancing the Needs of Water Use, 133–64. New York, NY: Springer New York, 1989. http://dx.doi.org/10.1007/978-1-4612-3496-8_6.

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Al Arni, Saleh S., and Mahmoud M. Elwaheidi. "Industrial Wastewater Treatment." In Concise Handbook of Waste Treatment Technologies, 89–109. First edition. | Boca Raton, FL: CRC Press, 2021.: CRC Press, 2020. http://dx.doi.org/10.4324/9781003112266-10.

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Al Arni, Saleh S., and Mahmoud M. Elwaheidi. "Industrial Wastewater Treatment." In Concise Handbook of Waste Treatment Technologies, 89–109. First edition. | Boca Raton, FL: CRC Press, 2021.: CRC Press, 2020. http://dx.doi.org/10.1201/9781003112266-10.

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Bwapwa, J. K., and B. F. Bakare. "Industrial Wastewater Treatment." In Removal of Refractory Pollutants from Wastewater Treatment Plants, 13–32. Boca Raton: CRC Press, 2021. http://dx.doi.org/10.1201/9781003204442-2.

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Verma, Subhash, Varinder S. Kanwar, and Siby John. "Industrial Wastewater Treatment." In Environmental Engineering, 447–53. New York: CRC Press, 2022. http://dx.doi.org/10.1201/9781003231264-30.

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Theodore, Mary K., and Louis Theodore. "Industrial Wastewater Management." In Introduction to Environmental Management, 189–96. 2nd ed. Second Edition. | Boca Raton ; London: CRC Press, 2021. | “First edition published by CRC Press 2009”—T.p. verso.: CRC Press, 2021. http://dx.doi.org/10.1201/9781003171126-22.

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Islam, Md Didarul, Meem Muhtasim Mahdi, Md Arafat Hossain, and Md Minhazul Abedin. "Biological Wastewater Treatment Plants (BWWTPs) for Industrial Wastewaters." In Wastewater Treatment, 139–56. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003165057-12.

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Otoo, Miriam, Javier Mateo-Sagasta, and Ganesha Madurangi. "Economics of Water Reuse for Industrial, Environmental, Recreational and Potable Purposes." In Wastewater, 169–92. Dordrecht: Springer Netherlands, 2015. http://dx.doi.org/10.1007/978-94-017-9545-6_10.

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Gupta, A. K., and C. Sahoo. "Treatment of Industrial Wastewater." In Recent Trends in Modelling of Environmental Contaminants, 143–65. New Delhi: Springer India, 2014. http://dx.doi.org/10.1007/978-81-322-1783-1_6.

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Conference papers on the topic "Industrial wastewater"

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Wu, Yongming, Mi Deng, Lizhen Liu, Jianyong Wang, Jie Zhang, and Jinbao Wan. "Wastewater treatment processes for industrial organosilicon wastewater." In 2016 International Conference on Innovative Material Science and Technology (IMST 2016). Paris, France: Atlantis Press, 2016. http://dx.doi.org/10.2991/imst-16.2016.9.

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Юй, Шуайсянь. "REMOVAL OF AMMONIA NITROGEN FROM INDUSTRIAL WASTEWATER." In Фундаментальные и прикладные исследования. Актуальные проблемы и достижения: сборник статей всероссийской научной конференции (Санкт­Петербург, Октябрь 2022). Crossref, 2022. http://dx.doi.org/10.37539/1011.2022.22.92.002.

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В этой статье рассматриваются несколько методов снижения содержания аммонийного азота в промышленных сточных водах в настоящее время. Обсуждаются методы снижения содержания аммонийного азота в сточных водах промышленных предприятий различных отраслей. В статье представлен обзор области применения, а также преимущества и недостатки каждого из этих методов в инженерном деле. This article discusses several methods for reducing ammoniacal nitrogen in industrial wastewater at present. Methods to reduce ammonia nitrogen in industrial wastewater from various industries are discussed. The article gives an overview of the application, as well as the advantages and disadvantages of each of these methods in engineering.
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Xiao, Nan, Litang Qin, Xin Zhang, Yanhong Li, and Fan Zhang. "Industrial wastewater biological toxicity research status." In 2016 5th International Conference on Energy and Environmental Protection (ICEEP 2016). Paris, France: Atlantis Press, 2016. http://dx.doi.org/10.2991/iceep-16.2016.90.

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Murphy, R. Jerry, and Paul A. Bizier. "Pretreatment of Industrial Oil Contact Wastewater." In World Water and Environmental Resources Congress 2001. Reston, VA: American Society of Civil Engineers, 2001. http://dx.doi.org/10.1061/40569(2001)472.

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Vinatoru, M. "Control solutions of aerobic industrial wastewater treatment." In 2010 International Joint Conference on Computational Cybernetics and Technical Informatics. IEEE, 2010. http://dx.doi.org/10.1109/icccyb.2010.5491300.

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Zhian, Hassan. "FILTERING WASTEWATER INDUSTRIAL USING OF ELECTROCOAGULATION METHOD." In SGEM2011 11th International Multidisciplinary Scientific GeoConference and EXPO. Stef92 Technology, 2011. http://dx.doi.org/10.5593/sgem2011/s20.128.

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Tsatiris, Dimitris, and Dimitris Sidiras. "Industrial wastewater treatment in fixed-bed systems." In INTERNATIONAL CONFERENCE OF COMPUTATIONAL METHODS IN SCIENCES AND ENGINEERING 2009: (ICCMSE 2009). AIP, 2012. http://dx.doi.org/10.1063/1.4772108.

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Hajar, Ibnu, Fadarina, Mustain Zamhari, and Selastia Yuliati. "Tofu Industrial Wastewater Treatment by Electrocoagulation Method." In 4th Forum in Research, Science, and Technology (FIRST-T1-T2-2020). Paris, France: Atlantis Press, 2021. http://dx.doi.org/10.2991/ahe.k.210205.008.

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"ADVANCED CONTROL OF AEROBIC INDUSTRIAL WASTEWATER TREATMENT." In 4th International Conference on Informatics in Control, Automation and Robotics. SciTePress - Science and and Technology Publications, 2007. http://dx.doi.org/10.5220/0001627401650170.

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Li, Xu, Guofeng Zheng, Jiange Hu, and Yili Li. "The design of automobile industrial wastewater treatment process." In 2011 International Conference on Electrical and Control Engineering (ICECE). IEEE, 2011. http://dx.doi.org/10.1109/iceceng.2011.6058346.

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Reports on the topic "Industrial wastewater"

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Morgan, James H., and Mary K. Fields. Missouri Industrial Wastewater System Characterization and Analysis, Whiteman Air Force Base. Fort Belvoir, VA: Defense Technical Information Center, March 1998. http://dx.doi.org/10.21236/ada343065.

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David B. Frederick. 2010 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site's Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2011. http://dx.doi.org/10.2172/1013724.

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Mike Lewis. 2013 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site’s Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2014. http://dx.doi.org/10.2172/1129940.

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Cafferty, Kara Grace. 2016 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site’s Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2017. http://dx.doi.org/10.2172/1364100.

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Lewis, Michael G. 2014 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site’s Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2015. http://dx.doi.org/10.2172/1178363.

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David Frederick. 2011 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site's Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2012. http://dx.doi.org/10.2172/1035893.

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Mike Lewis. 2012 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site?s Materials and Fuels Complex Industrial Waste Ditch and Industrial Waste Pond. Office of Scientific and Technical Information (OSTI), February 2013. http://dx.doi.org/10.2172/1064047.

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Cline, J. E., P. F. Sullivan, M. A. Lovejoy, J. Collier, and C. D. Adams. Ozone/UV treatment to enhance biodegradation of surfactants in industrial wastewater. CRADA final report. Office of Scientific and Technical Information (OSTI), October 1996. http://dx.doi.org/10.2172/666205.

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Lewis, Mike. Idaho National Laboratory Research Center Renewal Application for the Industrial Wastewater Acceptance Permit Number IF-8733-54171-1. Office of Scientific and Technical Information (OSTI), January 2018. http://dx.doi.org/10.2172/1467115.

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Mike Lewis. 2013 Annual Industrial Wastewater Reuse Report for the Idaho National Laboratory Site’s Advanced Test Reactor Complex Cold Waste Pond. Office of Scientific and Technical Information (OSTI), February 2014. http://dx.doi.org/10.2172/1129937.

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You might also be interested in the extended bibliographies on the topic 'Industrial wastewater' for particular source types:
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