Analytical methods for the determination of inorganic contaminants in fuels.
\\n\\n
IntechOpen was founded by scientists, for scientists, in order to make book publishing accessible around the globe. Over the last two decades, this has driven Open Access (OA) book publishing whilst levelling the playing field for global academics. Through our innovative publishing model and the support of the research community, we have now published over 5,700 Open Access books and are visited online by over three million academics every month. These researchers are increasingly working in broad technology-based subjects, driving multidisciplinary academic endeavours into human health, environment, and technology.
\\n\\nBy listening to our community, and in order to serve these rapidly growing areas which lie at the core of IntechOpen's expertise, we are launching a portfolio of Open Science journals:
\\n\\nAll three journals will publish under an Open Access model and embrace Open Science policies to help support the changing needs of academics in these fast-moving research areas. There will be direct links to preprint servers and data repositories, allowing full reproducibility and rapid dissemination of published papers to help accelerate the pace of research. Each journal has renowned Editors in Chief who will work alongside a global Editorial Board, delivering robust single-blind peer review. Supported by our internal editorial teams, this will ensure our authors will receive a quick, user-friendly, and personalised publishing experience.
\\n\\n"By launching our journals portfolio we are introducing new, dedicated homes for interdisciplinary technology-focused researchers to publish their work, whilst embracing Open Science and creating a unique global home for academics to disseminate their work. We are taking a leap toward Open Science continuing and expanding our fundamental commitment to openly sharing scientific research across the world, making it available for the benefit of all." Dr. Sara Uhac, IntechOpen CEO
\\n\\n"Our aim is to promote and create better science for a better world by increasing access to information and the latest scientific developments to all scientists, innovators, entrepreneurs and students and give them the opportunity to learn, observe and contribute to knowledge creation. Open Science promotes a swifter path from research to innovation to produce new products and services." Alex Lazinica, IntechOpen founder
\\n\\nIn conclusion, Natalia Reinic Babic, Head of Journal Publishing and Open Science at IntechOpen adds:
\\n\\n“On behalf of the journal team I’d like to thank all our Editors in Chief, Editorial Boards, internal supporting teams, and our scientific community for their continuous support in making this portfolio a reality - we couldn’t have done it without you! With your support in place, we are confident these journals will become as impactful and successful as our book publishing program and bring us closer to a more open (science) future.”
\\n\\nWe invite you to visit the journals homepage and learn more about the journal’s Editorial Boards, scope and vision as all three journals are now open for submissions.
\\n\\nFeel free to share this news on social media and help us mark this memorable moment!
\\n\\n\\n"}]',published:!0,mainMedia:{caption:"",originalUrl:"/media/original/237"}},components:[{type:"htmlEditorComponent",content:'
After years of being acknowledged as the world's leading publisher of Open Access books, today, we are proud to announce we’ve successfully launched a portfolio of Open Science journals covering rapidly expanding areas of interdisciplinary research.
\n\n\n\nIntechOpen was founded by scientists, for scientists, in order to make book publishing accessible around the globe. Over the last two decades, this has driven Open Access (OA) book publishing whilst levelling the playing field for global academics. Through our innovative publishing model and the support of the research community, we have now published over 5,700 Open Access books and are visited online by over three million academics every month. These researchers are increasingly working in broad technology-based subjects, driving multidisciplinary academic endeavours into human health, environment, and technology.
\n\nBy listening to our community, and in order to serve these rapidly growing areas which lie at the core of IntechOpen's expertise, we are launching a portfolio of Open Science journals:
\n\nAll three journals will publish under an Open Access model and embrace Open Science policies to help support the changing needs of academics in these fast-moving research areas. There will be direct links to preprint servers and data repositories, allowing full reproducibility and rapid dissemination of published papers to help accelerate the pace of research. Each journal has renowned Editors in Chief who will work alongside a global Editorial Board, delivering robust single-blind peer review. Supported by our internal editorial teams, this will ensure our authors will receive a quick, user-friendly, and personalised publishing experience.
\n\n"By launching our journals portfolio we are introducing new, dedicated homes for interdisciplinary technology-focused researchers to publish their work, whilst embracing Open Science and creating a unique global home for academics to disseminate their work. We are taking a leap toward Open Science continuing and expanding our fundamental commitment to openly sharing scientific research across the world, making it available for the benefit of all." Dr. Sara Uhac, IntechOpen CEO
\n\n"Our aim is to promote and create better science for a better world by increasing access to information and the latest scientific developments to all scientists, innovators, entrepreneurs and students and give them the opportunity to learn, observe and contribute to knowledge creation. Open Science promotes a swifter path from research to innovation to produce new products and services." Alex Lazinica, IntechOpen founder
\n\nIn conclusion, Natalia Reinic Babic, Head of Journal Publishing and Open Science at IntechOpen adds:
\n\n“On behalf of the journal team I’d like to thank all our Editors in Chief, Editorial Boards, internal supporting teams, and our scientific community for their continuous support in making this portfolio a reality - we couldn’t have done it without you! With your support in place, we are confident these journals will become as impactful and successful as our book publishing program and bring us closer to a more open (science) future.”
\n\nWe invite you to visit the journals homepage and learn more about the journal’s Editorial Boards, scope and vision as all three journals are now open for submissions.
\n\nFeel free to share this news on social media and help us mark this memorable moment!
\n\n\n'}],latestNews:[{slug:"webinar-introduction-to-open-science-wednesday-18-may-1-pm-cest-20220518",title:"Webinar: Introduction to Open Science | Wednesday 18 May, 1 PM CEST"},{slug:"step-in-the-right-direction-intechopen-launches-a-portfolio-of-open-science-journals-20220414",title:"Step in the Right Direction: IntechOpen Launches a Portfolio of Open Science Journals"},{slug:"let-s-meet-at-london-book-fair-5-7-april-2022-olympia-london-20220321",title:"Let’s meet at London Book Fair, 5-7 April 2022, Olympia London"},{slug:"50-books-published-as-part-of-intechopen-and-knowledge-unlatched-ku-collaboration-20220316",title:"50 Books published as part of IntechOpen and Knowledge Unlatched (KU) Collaboration"},{slug:"intechopen-joins-the-united-nations-sustainable-development-goals-publishers-compact-20221702",title:"IntechOpen joins the United Nations Sustainable Development Goals Publishers Compact"},{slug:"intechopen-signs-exclusive-representation-agreement-with-lsr-libros-servicios-y-representaciones-s-a-de-c-v-20211123",title:"IntechOpen Signs Exclusive Representation Agreement with LSR Libros Servicios y Representaciones S.A. de C.V"},{slug:"intechopen-expands-partnership-with-research4life-20211110",title:"IntechOpen Expands Partnership with Research4Life"},{slug:"introducing-intechopen-book-series-a-new-publishing-format-for-oa-books-20210915",title:"Introducing IntechOpen Book Series - A New Publishing Format for OA Books"}]},book:{item:{type:"book",id:"509",leadTitle:null,fullTitle:"Biomedical Science, Engineering and Technology",title:"Biomedical Science, Engineering and Technology",subtitle:null,reviewType:"peer-reviewed",abstract:"This innovative book integrates the disciplines of biomedical science, biomedical engineering, biotechnology, physiological engineering, and hospital management technology. Herein, Biomedical science covers topics on disease pathways, models and treatment mechanisms, and the roles of red palm oil and phytomedicinal plants in reducing HIV and diabetes complications by enhancing antioxidant activity. Biomedical engineering coves topics of biomaterials (biodegradable polymers and magnetic nanomaterials), coronary stents, contact lenses, modelling of flows through tubes of varying cross-section, heart rate variability analysis of diabetic neuropathy, and EEG analysis in brain function assessment. Biotechnology covers the topics of hydrophobic interaction chromatography, protein scaffolds engineering, liposomes for construction of vaccines, induced pluripotent stem cells to fix genetic diseases by regenerative approaches, polymeric drug conjugates for improving the efficacy of anticancer drugs, and genetic modification of animals for agricultural use. Physiological engineering deals with mathematical modelling of physiological (cardiac, lung ventilation, glucose regulation) systems and formulation of indices for medical assessment (such as cardiac contractility, lung disease status, and diabetes risk). Finally, Hospital management science and technology involves the application of both biomedical engineering and industrial engineering for cost-effective operation of a hospital.",isbn:null,printIsbn:"978-953-307-471-9",pdfIsbn:"978-953-51-4376-5",doi:"10.5772/1020",price:169,priceEur:185,priceUsd:219,slug:"biomedical-science-engineering-and-technology",numberOfPages:904,isOpenForSubmission:!1,isInWos:1,isInBkci:!0,hash:"eec1ae8717629372ed7f0c0499dee14c",bookSignature:"Dhanjoo N. 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Kye has written in the article Professor with a mission, [Dhanjoo Ghista] is a professor of professors, a world authority in biomedical engineering and physics, author or editor of several textbooks in subjects ranging from cardiovascular physics to African Rural Development and inventor of life-saving implant devices. A pioneer of research into the effect of space travel on astronauts, his work as the founder and leading exponent of the new science of societal engineering has received recognition from academics and institutions alike.\r\n\r\nAlong with having being editor-in-chief of Automedica (an international journal of high-tech medicine), Prof. Dr. Dhanjoo N. Ghista has published over 450 works in the fields of engineering science, biomedical engineering, medical science, and social sciences. 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\r\n\tSensory processing plays an integral role in the interaction and adaptation by which an individual navigates through a stimulus-loaded environment. Although intensive research of sensory processing has accumulated a large body of knowledge over the years, the key issues such as where, when and how the human neural system processes, integrates and influences environmental information to produce personal experiences and images of reality, are still open. As neurocognitive theories of sensory processing rapidly change and develop with novel research findings, there is a great potential to consider the current extent to which these findings can help in understanding the complex interfering of surround stimuli with an individual’s processing of elicited cognitive responses.
\r\n\r\n\tThe book Integration and Representation of Sensory Processes aims to disseminate the latest research breakthroughs in the field of basic and clinical neurophysiology of sensory processing and multisensory integration. The book intends to introduce novel models of sensory processing and explore functional and effective connectivity between brain areas underlying sensory responses and the multimodal integration with possible clinical implications of these findings in the diagnosis and treatment of neurological and psychiatric disorders. The methods presented to assess human neural systems involved in sensory processing and the generations of perception cover a range of functional neuroimaging approaches including electroencephalography (EEG), magnetoencephalography (MEG), positron emission tomography (PET) and functional magnetic resonance imaging (fMRI). These techniques have created the opportunity to explore the relationship between stimulus properties, stimulus representation in the brain, and their connection with perceptual attributes more directly. Finally, applications of neurophysiological sensory processing results will be discussed, including the state-of-the-art development of brain-machine interfaces.
",isbn:null,printIsbn:"979-953-307-X-X",pdfIsbn:null,doi:null,price:0,priceEur:0,priceUsd:0,slug:null,numberOfPages:0,isOpenForSubmission:!1,isSalesforceBook:!1,hash:"b58da2a096851c1ff54ab87fd7ad88ed",bookSignature:"Ph.D. Sanja Josef Golubic",publishedDate:null,coverURL:"https://cdn.intechopen.com/books/images_new/8932.jpg",keywords:"Auditory and Visual Sensory Processing, Gating Phenomena, Multisensory Integration, Sensory Processing Disorders, Gating Processing Stream, Ventral Processing Stream, Dorsal Processing Stream, Cortical Projection Areas, Sensory processing disorder, Parkinson's disease (PD), Huntington's disease (HD), Dystonia",numberOfDownloads:null,numberOfWosCitations:0,numberOfCrossrefCitations:null,numberOfDimensionsCitations:null,numberOfTotalCitations:null,isAvailableForWebshopOrdering:!0,dateEndFirstStepPublish:"July 2nd 2020",dateEndSecondStepPublish:"July 23rd 2020",dateEndThirdStepPublish:"September 21st 2020",dateEndFourthStepPublish:"December 10th 2020",dateEndFifthStepPublish:"February 8th 2021",remainingDaysToSecondStep:"2 years",secondStepPassed:!0,currentStepOfPublishingProcess:5,editedByType:null,kuFlag:!1,biosketch:"Dr. Josef Golubic's latest highlight contribution to the field includes resolving 30-years long enigma of neural network underlying auditory sensory gating; disclosing a new, fast cortical pathway which links prefrontal cortex to primary sensory areas within first 100 milliseconds after stimulation, and finally revealing a discrete individual biomarker of Alzheimer’s disease with the potential to detect the disease in its preclinical stage.",coeditorOneBiosketch:null,coeditorTwoBiosketch:null,coeditorThreeBiosketch:null,coeditorFourBiosketch:null,coeditorFiveBiosketch:null,editors:[{id:"225125",title:"Ph.D.",name:"Sanja",middleName:null,surname:"Josef Golubic",slug:"sanja-josef-golubic",fullName:"Sanja Josef Golubic",profilePictureURL:"https://mts.intechopen.com/storage/users/225125/images/system/225125.png",biography:"Sanja Josef Golubic is a senior research and teaching assistant (postdoctoral fellow) at the Department of Physics, Faculty of Science, University of Zagreb. \r\n\r\nHer academic qualifications include a Ph.D. in cognitive neurodynamics and M.Sc. in theoretical physics. 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The latest highlight contributions to the field include resolving 30-years long enigma of neural network underlying auditory sensory gating; disclosing a new, fast cortical pathway which links prefrontal cortex to primary sensory areas within first 100 milliseconds after stimulation, and finally revealing a discrete individual biomarker of Alzheimer’s disease with the potential to detect the disease in its preclinical stage.",institutionString:"Department of Physics, Faculty of Science, University of Zagreb",position:null,outsideEditionCount:0,totalCites:0,totalAuthoredChapters:"1",totalChapterViews:"0",totalEditedBooks:"1",institution:{name:"University of Zagreb",institutionURL:null,country:{name:"Croatia"}}}],coeditorOne:null,coeditorTwo:null,coeditorThree:null,coeditorFour:null,coeditorFive:null,topics:[{id:"18",title:"Neuroscience",slug:"life-sciences-neuroscience"}],chapters:null,productType:{id:"1",title:"Edited Volume",chapterContentType:"chapter",authoredCaption:"Edited by"},personalPublishingAssistant:{id:"247865",firstName:"Jasna",lastName:"Bozic",middleName:null,title:"Ms.",imageUrl:"https://mts.intechopen.com/storage/users/247865/images/7225_n.jpg",email:"jasna.b@intechopen.com",biography:"As an Author Service Manager, my responsibilities include monitoring and facilitating all publishing activities for authors and editors. From chapter submission and review to approval and revision, copyediting and design, until final publication, I work closely with authors and editors to ensure a simple and easy publishing process. I maintain constant and effective communication with authors, editors and reviewers, which allows for a level of personal support that enables contributors to fully commit and concentrate on the chapters they are writing, editing, or reviewing. I assist authors in the preparation of their full chapter submissions and track important deadlines and ensure they are met. I help to coordinate internal processes such as linguistic review, and monitor the technical aspects of the process. As an ASM I am also involved in the acquisition of editors. 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Ethyl alcohol (ethanol) is considered to be a highly viable alternative fuel. Its production from biomass means that it can provide a source of energy that is both clean and renewable. The inclusion of ethanol as a component of gasoline can help to reduce problems of pollution in many regions, since it eliminates the needto use tetraethyl lead (historically notorious as a highly toxic trace component of the atmosphere in major cities) as an anti-knock additive.
The quantitative monitoring of metal elements in fuels (including gasoline, alcohol, and diesel) is important from an economic perspective in the fuel industry as well as in the areas of transport and environment. The presence of metalspecies (ions or organometallic compounds) in automotive fuels can cause engine corrosion, reduce performance, and contribute to environmental contamination [2-5].
The low concentrations of metals in fuels typically require the use of sensitive spectrometric analytical techniques for the purposes of quality control. Atomic absorption spectrometry (AAS) can be applied for the quantitative determination of many elements (metals and semi-metals) in a wide variety of media including fuels, foodstuffs, and biological, environmental, and geological materials, amongst others. The principle of the technique is based on measurement of the absorption of optical radiation, emitted from a source, by ground-state atoms in the gas phase. Atomization can be achieved using a flame, electrothermal heating, or specific chemical reaction (such as the generation of Hg cold vapor). Electrothermalatomizers include graphite tubes, tungsten filaments, and quartz tubes (for atomization of hydrides), as well as metal or ceramic tubes. Flame atomic absorption spectrometry (FAAS) is mostly used for elemental analysis at higher concentration levels, of the order of mg L-1[3-5]. Table 1 lists some of the published studies concerning the application of AAS for determination of metals in fuels.
\n\t\t\t\t | \n\t\t\t\n\t\t\t\t | \n\t\t\t\n\t\t\t\t | \n\t\t\t\n\t\t\t\t | \n\t\t
Graphite furnace atomic absorption spectrometry (GFAAS) | \n\t\t\tFuel oil | \n\t\t\tMicrowave digestion | \n\t\t\t6 | \n\t\t
Flame atomic absorption spectrometry | \n\t\t\tFuel oil | \n\t\t\tWet digestion | \n\t\t\t7 | \n\t\t
Atomic fluorescence spectrometry with cold vapor generation | \n\t\t\tGasoline and other petroleum derivatives | \n\t\t\tWet digestion | \n\t\t\t8 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tFuel oil | \n\t\t\tMicrowave digestion | \n\t\t\t9 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tCrude fuel oil | \n\t\t\tDilution in xylene/I2, wet and microwave digestion | \n\t\t\t10 | \n\t\t
Flame atomic absorption spectrometry | \n\t\t\tEngine oil | \n\t\t\tWet digestion | \n\t\t\t11 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tFuel oils and naphtha | \n\t\t\tOil-water emulsion | \n\t\t\t12 | \n\t\t
Inductively coupled plasma mass spectrometry (ICP-MS) | \n\t\t\tGasoline | \n\t\t\tEmulsion with Triton X-100 surfactant | \n\t\t\t13 | \n\t\t
Flame atomic absorption spectrometry | \n\t\t\tEthyl alcohol | \n\t\t\tDilution in HNO3\n\t\t\t | \n\t\t\t5 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tEthyl alcohol | \n\t\t\tDilution in HNO3\n\t\t\t | \n\t\t\t3,4 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tEthyl alcohol | \n\t\t\tDilution in HNO3\n\t\t\t | \n\t\t\t2 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tEthyl alcohol and acids | \n\t\t\tDilution in HNO3\n\t\t\t | \n\t\t\t14 | \n\t\t
Graphite furnace atomic absorption spectrometry with a high-resolution continuum source (HR-CS-GFAAS) | \n\t\t\tCrude oil | \n\t\t\tOil-water emulsion | \n\t\t\t15 | \n\t\t
Atomic absorption spectrometry with thermal nebulization in a tube heated in a flame (TS-FF-AAS) | \n\t\t\tEthyl alcohol fuel and gasoline | \n\t\t\tDilution in HNO3/oil-water emulsion | \n\t\t\t16 | \n\t\t
Graphite furnace atomic absorption spectrometry with a high-resolution continuum source | \n\t\t\tCrude oil | \n\t\t\tOil-water emulsion | \n\t\t\t17 | \n\t\t
Atomic absorption spectrometry | \n\t\t\tGasoline, diesel, ethyl alcohol and biodiesel | \n\t\t\t- (Review) | \n\t\t\t18 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tEthyl alcohol and acids | \n\t\t\tDirect determination | \n\t\t\t19 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tBiodiesel | \n\t\t\tMicrowave digestion and emulsion | \n\t\t\t1 | \n\t\t
Flame atomic absorption spectrometry | \n\t\t\tEthyl alcohol | \n\t\t\tSolid phase extraction | \n\t\t\t20 | \n\t\t
Graphite furnace atomic absorption spectrometry | \n\t\t\tBiodiesel | \n\t\t\tEmulsion | \n\t\t\t21 | \n\t\t
Atomic absorption spectrometry with vapor generation (VP-FAAS) | \n\t\t\tEthyl alcohol | \n\t\t\tTreatment with acid under UV irradiation | \n\t\t\t22 | \n\t\t
Analytical methods for the determination of inorganic contaminants in fuels.
The thermospray (TS) technique was originally developed by Vestal et al.in 1978 [23]as an interface between liquid chromatography and mass spectrometry. In atomic absorption spectrometry, the tube was heated electrically in order to maintain a constant temperature, which restricted use of the method to only a few elements. However, Gáspárand Berndt (2000) proposed the TS-FF-AAS procedure, in which a metal tube is positioned above the flame of the atomic absorption spectrometer, as a reactor. The sample solution is transported through a metal capillary, connected to the tube, and heated simultaneously by the flame. On reaching the hot tip of the capillary, the liquid partially vaporizes, forming an aerosol. In turn, the aerosol is vaporized within the tube, producing an atomic cloud that absorbs the radiation emitted by the lamp.
The TS-FF-AAS method was used as an interface between high performance liquid chromatography (HPLC) and FAAS, employing a flow injection system [25-60].
The objective of this work is to describe the analysis of Cu present in hydrated ethyl alcohol fuel (HEAF) using the technique of atomic absorption spectrometry with thermal nebulization in a tube heated in a flame (TS-FF-AAS). The atomizers used were a metal tube (Ni-Cr alloy) and a ceramic tube (Al2O3).
The instrumentation consisted of an atomic absorption spectrometer fitted with a flame atomizer (Perkin-Elmer, model AAnalyst 100), a hollow cathode Cu lamp (λ = 324.8 nm, slit width = 0.7 nm,i = 15 mA), with an air/acetylene (4:2 ratio) flame gas mixture, and background correction using a deuterium lamp. Other equipment comprised an analytical balance (Sartorius BL 2105) and a peristaltic pump (Ismatec, model ICP 8).
The TS-FF-AAS assembly employed a Rheodyne RE9725 injection valve, PEEK tubing, and a ceramic thermocouple insulator capillary (OMEGATITE450, OMEGA, USA). The capillary wascomposed of Al2O3(>99.8%), resistant to temperatures up to 1900 °C, with Øext= 1.6 mm and two orifices with Øint = 0.4 mm (this capillary provided better results than a stainless steel HPLC capillary, with less noise in the absorbance signal). The atomization tubes were a metal tube composed of Ni-Cr super-alloy (Inconel, length 100 mm, Øint = 10.0 mm, Øext = 12.0 mm, 6 orifices with Ø = 2.5 mm, perpendicular to an orifice with Ø = 2.0 mm), and a ceramic tube (99.9% Al2O3, length 100 mm, Øint = 10.0 mm, Øext = 12.0 mm, 6 orifices with Ø = 2.5 mm, perpendicular to an orifice with Ø = 2.0 mm).
Data acquisition employed the software MQDOS (Microquímica), and the absorbance values were proportional to the height of the transient signals.
The temperature in the interior of the atomization tube was measured in two ways. The first method employed a thermocouple with an earthed connection, positioned adjacent to the metal tube, oriented towards the orifice where the ceramic capillary used to introduce the sample into the atomizer was located. The temperature measured for the metal tube was 983 ± 1°C. Secondly, the thermocouple with connection exposed was positioned adjacent to the ceramic capillary within the tube, where a temperature of between 1030 °C and 1060°C was measured, at which the tube glowed ruby-red above the flame [16,40,45,54].
When 50 μL of HNO3 (~0.1 mol L-1) was injected at a rate of approximately 1.5 mL min-1,there was a temperature reduction of around 50°C, due to cooling of the tube by the solution, followed by a rapid return to the maximum temperature range.
Working standard solutions were prepared from a stock 1000 mg L-1 copper standard solution (spectroscopic grade), by dilution in 0.14 mol L-1 HNO3 (Synth).
The HEAF samples were prepared by mixing the fuel with an equal volume of 0.14 mol L-1 HNO3,with final volumes of 50 mL [3-5]. Subsequent quantification employed the standard additions procedure.
A schematic diagram of the TS-FF-AAS system is shown in Figure 1.
It is recommended that the Inconel tube should only be positioned above the burner head after lighting the flame, to avoid the possibility of an explosion within the tube due to gas accumulation. The TS-FF-AAS system was therefore first assembled, after which the spectrometer flame was ignited immediately after opening the gas valves to avoid any explosion risk. This procedure facilitated the positioning of the tube above the burner head, which was performed while the flame was extinguished. All analyses employed a fixed volume of sample, injected into the flow of air as the carrier, since previous work has shown that injection using carrier solutions results in greater sample dilution and dispersion [40,45,54,58].
Schematic arrangement of the TS-FF-AAS system (adapted from Davies & Berndt 2003[59].
The sample was introduced into the system using a manual Rheodyne valve (Figure 1), after which it was transported to the ceramic capillary in the flow of air. Since the capillary was heated simultaneously with the metal or ceramic reactor tube, the liquid was partially vaporized, forming a thermospray, and atomization occurred on arrival in the tube, generating a transient signal that was captured and stored by the software. The determination employed the height of the transient signal peak.
The influences of the carrier flow rate (in the range 9.0-18.0 mL min-1) and the sample volume (50, 100, and 200μL) were evaluated using a standard of 200μg Cu L–1.
After optimization of the system, analytical curves were constructed in the concentration range 0.1-0.4 mg Cu L-1 in 0.14mol L-1 HNO3. Additions of analyte were made to the sample mixed with an equal volume of 0.14 mol L-1 HNO3. The detection limit (DL) was calculated from 12 blank readings for each type of tube (metal or ceramic).
Good peak reproducibility was achieved when samples were injected into the air flow as carrier. When samples were injected into 0.14 mol L-1 HNO3, used as the carrier, there was a rise in the baseline (as expected, due to increase of the blank), followed by a fall due to cooling of the metal or ceramic tubes. This cooling was significant, since no transient signals were obtained following injection of standards, indicating that the temperature within the tubes was insufficient to atomize the analyte, which remained dispersed in the carrier solution. This confirmed the findings of earlier work that the use of air (or other gas) as the carrier avoids dilution and dispersion of the sample. Here, all analyses were performed using air as the carrier, not only because it was less expensive than use of a solution, and minimized waste generation, but also because it enabled the TS-FF-AAS system to be used to determine copper, which would not have been possible using a solution as the carrier.
Figure 2 shows the influence of the carrier (air) flow rate, in the range 9.0-18.0 mL min-1, on the absorbance values obtained using 50 μL of a standard of 200 μg Cu L-1in 0.14 mol L-1 HNO3, using both tubes.In the case of the metal tube, lower absorbance values were obtained at low flow rates, because the sample arrived slowly at the atomizer,increasing the measurement duration and resulting in an unpredictable and erratic vaporization. Hence, as the flow rate was increased, the absorbance also increased due to a more homogeneous vaporization of the sample [23,27,58].
Influence of carrier (air) flow rate on the absorbance obtained for 50 μLof a solution of200 μg Cu L-1 in 0.14mol L-1HNO3, using the metal and ceramic tubes.
This increase proceeded up to a carrier flow rate of 12.0 mL min-1, above which there was no significant variation in absorbance. The highest absorbance value was obtained at a flow rate of 18.0 mL min-1, which was therefore selected as the best flow rate to use with the metal tube.
When the ceramic tube was used, maximum absorbance was achieved at a carrier flow rate of 9.0 mL min-1. At higher flow rates, the residence time of the liquid in the heated section of the ceramic capillary was considerably diminished, reducing the time available for evaporation of the liquid, so that the sample was not delivered in the form of vapor/aerosol, but rather as a flow of liquid. The temperature within the tube decreased, and the color of the tube changed from ruby-red to opaque grey. It was also possible to see droplets emerging from the atomizer tube. Hence, the absorbance values did not increase, while greater variability in the signal resulted in elevated standard deviation values. A flow rate of 3.0 mL min-1was selected, at which the absorbance signal was maximized, and the standard deviation was minimized.
Influence of sample volume on the absorbances obtained for a solution of 200 μg CuL-1in0.14mol L-1HNO3, using carrier flow rates of 9.0 and 18.0 mL min-1for the ceramic and metal tubes, respectively.
The sample volume was varied between 50 and 200 μL, using carrier flow rates of 18.0 and 9.0 mL min-1 for the metal and ceramic tubes, respectively. The results (Figure 3) revealed that for both tubes a sample volume of 50 μL generated the highest absorbance value, with a low standard deviation, reflecting good repeatability in the experimental measurements. When 100 μL of sample was used, there was a slight cooling of the ceramic capillary, and consequently of the atomization tubes, while there was no increase in the absorbance values. At a sample volume of 200 μL, the ceramic capillary and the tube were substantially cooled, and there was no homogeneous thermospray formation, with erratic generation of droplets that acted to disperse the light radiation (probably to a large degree, since the deuterium lamp was unable to fully correct the resulting background signal). The unpredictable atomization resulted in very high standard deviation values. Using air as the carrier, a sample volume of 50 μL was selected for the subsequent measurements, due to greater atomization homogeneity, satisfactory absorbance for a 30 mg Cu L-1 standard, and a low SD value.
Figure 4 illustrates the results obtained for the analytical curve in the concentration range 0.1-0.4 μg Cu L–1 in 0.14 mol L-1HNO3, using the optimized conditions of the TS-FF-AAS system. The transient signals were repeatable, and (for both tubes) the curve was linear in the concentration range studied. A two-fold greater sensitivity was achieved using the ceramic tube.
Regression lines fitted to the analytical curves of Cu obtained using the ceramic tube (a) and the metal tube (b) Equations of the lines: A = 1.16x10-2 + 5.27x10-4(Cu) (ceramic tube);A = 1.20x10-3 + 2.91x10-4(Cu) (metal tube).
Figure 5 illustrates the results obtained for the analytical curves constructed using concentrations of Cu in the range 100-400 μg L–1, with additions of analytein 0.14 mol L-1 HNO3 to equal volumes of sample, under the optimized TS-FF-AAS system conditions. The presence of 75.8 μg Cu L-1 in the sample was calculated from curve (a), obtained using the ceramic tube. This value was slightly above the detection limit (Table 1), although below the concentration of the first point of the analytical curve. In the case of the metal tube (curve (b)), a Cu concentration of 80.0 μg L-1 was below the detection limit for this tube, but was nevertheless in agreement with the result obtained for the ceramic tube.
Regression lines fitted to the analytical curves of Cu in 1:1 mixtures of fuel samples and standards prepared in 0.14 mol L-1 HNO3, obtained using the ceramic tube (a) and the metal tube (b) Equations of the lines: A = 1.00x10-2 + 1.32x10-4 (Cu) (ceramic tube); A = 1.16x10-2 + 1.45x10-4 (Cu) (metal tube).
\n\t\t\t | \n\t\t\t\t | \n\t\t\t\n\t\t\t\t | \n\t\t\t|
HNO3\n\t\t\t | \n\t\t\tDetection limit, DL (μg L-1) | \n\t\t\t55.6 | \n\t\t\t56.0 | \n\t\t
Characteristic concentration, Co (μg L-1) | \n\t\t\t8.35 | \n\t\t\t15.1 | \n\t\t|
Analytical curve interval (μg L-1) | \n\t\t\t100 – 400 | \n\t\t||
Correlation coefficient (r) | \n\t\t\t0.9930 | \n\t\t\t0.9978 | \n\t\t|
Analytical frequency (h-1) | \n\t\t\t26 | \n\t\t\t100 | \n\t\t|
HEAF | \n\t\t\tDetection limit, DL (μg L-1) | \n\t\t\t64.5 | \n\t\t\t128 | \n\t\t
Characteristic concentration, Co (μg L-1) | \n\t\t\t33.3 | \n\t\t\t30.3 | \n\t\t|
Analytical curve interval (μg L-1) | \n\t\t\t100 – 400 | \n\t\t||
Correlation coefficient (r) | \n\t\t\t0.9918 | \n\t\t\t0.9927 | \n\t\t|
Analytical frequency (h-1) | \n\t\t\t53 | \n\t\t\t82 | \n\t\t
Analytical characteristics for determination of Cu using the TS-FF-AAS system with ceramic and metal tubes.
The analytical parameters obtained for the determination of Cu under the optimized conditions of the TS-FF-AAS system are provided in Table 2. The analytical curves were linear for a concentration range of 100-400 μg Cu L-1 in 0.14 mol L-1 HNO3. The system could be considered to be sensitive, with characteristic concentrations of 8 and 15 μg Cu L-1 for the ceramic and metal tubes, respectively, and analysis frequencies (using HNO3 medium) of 26 and 100 determinations per hour, respectively. Better analytical performance of the system was achieved using the ceramic tube, compared to the metal tube. The data showed that the TS-FF-AAS technique was more sensitive than FAAS, with nine-fold (ceramic tube) and five-fold (metal tube) increases in sensitivity, relative to FAAS with pneumatic nebulization, for which the characteristic concentration was 77 μg L-1. The increase in power of detectionobtained using the ceramic tube was around twice that for the metal tube. The sensitivity for determination of copper using the ceramic tube was therefore two-fold that obtained using the metal tube.
The TS-FF-AAS system can be used to determine copper at low concentrations, using either metal (Inconel) or ceramic (Al2O3) tubes as atomizers. Following optimization considering the most important experimental variables affecting atomization, these systems provided significantly improved detection limits for Cu determination, with nine-fold (ceramic tube) and five-fold (metal tube) increases in sensitivity, compared to traditional FAAS with pneumatic nebulization. The TS-FF-AAS technique is simple, fast, effective, and inexpensive. It requires low volumes of sample (as little as 50 μL) and reagents, and reduces waste generation. The method offers a useful new alternative for the determination of copper in alcohol.
The authors thank UFOP and CNPq for financial assistance.
During last few decades, there has been an increasing awareness among the scientific community about the impact of carrying out mining activities [1, 2]. Before implementing standard ore exploitation activities, potential contaminant species remain restrained inside the original rock, however, such situation changes once mining activities kickoff and valuable material along with other toxic species are mobilised throughout the atmosphere or other media such as surface- or ground-waters. Among the latter, Acid Mine Drainage (AMD) has arisen as one of the most relevant multidisciplinary challenges in the mining industry [3]. The AMD corresponds to an aqueous stream which appears spontaneously from the natural contact, and therefore the natural interaction, between the surface of the rocks (or mineral particles) exhibiting at their surface primarily metal sulphide structures, and water either in the form of vapour or liquid in conjunction with other atmospheric gases (Figure 1) [4, 5].
Scheme of acid mine drainage (AMD) production.
Perhaps the major difference between AMD and other sorts of pollution is that the former is not directly produced by mining activities. Mining activities would inevitably produce, to some extent, solid wastes and then, the environment in contact with them would eventually trigger the generation of AMD. In other words, the misplacing of solid wastes coming from anthropogenic mining activities in nature itself spontaneously transforms it into a different system with increased toxicity. In this context, the appearance of AMD depends largely on the local atmospheric conditions. For instance, higher humidity or rainy weather will favour the generation of AMD compared to dry conditions [4].
From a historical standpoint, one of the first reports indicating the generation of AMD was published in 1895 by F.G. Holman who glanced at the presence of a waterflow coming out from a small mine site in Forbestown, Sierra Nevada, California [6]. During AMD formation several physical, chemical, and biological phenomena are triggered while solid wastes and environment interact and are commonly summarised by many authors as simple as “weathering” [7, 8]. Weathering, though, is a wide concept that encompasses all the characteristics related to the environment including climate and biosphere. This makes it a bit too general to fully predict the specifics of AMD (timespan to appear, chemical composition, etc.) and its instantaneous or long-term impact on the mine site surrounding areas. The locations where mine sites are placed present a variety of different climates like desertic, Mediterranean, or other. Therefore, when carrying out any study on AMD prediction, prevention, treatment or other, the ambient conditions used will be crucial to get proper results [9].
Before examining the fundamentals behind the generation of AMD, a brief analysis of where AMD might be generated from a mineral processing perspective will be presented. There are many situations where AMD may appear across the mineral processing line, especially when solid wastes appear. For instance, it is well known that base metals occurrence covers a wide range of mineral structures such as oxides, sulphides, and intermediate phases [10]. Although oxide minerals bearing ores may also produce AMD due to their susceptibility to undertake leaching and metal hydrolysis steps in aqueous aerated conditions, sulphide-bearing minerals are considered the major ones responsible for it. In that context, AMD is mainly associated with base metals and coal beneficiation plants where sulphide minerals occur as valuable or gangue material [11]. Only for exemplification purposes, and given its worldwide relevancy, the copper sulphide pyrometallurgical beneficiation path will be discussed. The traditional copper sulphide line of process usually includes blasting, rock size reduction (crushing and milling) and mineral selective separation commonly froth flotation [12]. Figure 2 presents a block diagram of that line of ore processing, identifying the most relevant scenarios where AMD may be anticipated to take place.
Possible ore processing situations where AMD may appear, and the maximum diameter of rocks/particles involved in each scenario. Particle diameter is referred from [
From a practical perspective, it is all about sulphide-bearing material in the form of particles with different diameters being piled up which generate a certain natural porosity that will determine the access of atmospheric gases (or material weathering) towards the interior of the porous material. Different particle size distributions can be observed across the process line characterised in the picture by the maximum particle size only. Another common and better way to estimate a mean diameter biased to larger diameter values of a set of rocks or particles is through the Sauter mean diameter (
where,
Eq. (2) is normally preferred as it considers the whole population of rocks or particles which brings up the significance of a correct sampling procedure, another crucial aspect of AMD. The mean diameter of a population of rocks or particles is studied with different techniques depending on the relevant particle sizes. For instance, after blasting operation optical methods are widely used while for tailing materials sieving processes are preferred [15]. Nevertheless, particle size is not the only key variable to look at. The content of the valuable and gangue species present in the solid waste is also a variable to take into consideration. For instance, copper grades of sulphide minerals bearing ores fed to a concentrator usually contain around 0.8% copper leaving final tailings with about 0.1% of the metal [16]. Low-grade copper sulphide ores fed to dump leach operations contain copper grades between 0.1 and 0.3% and the extraction may reach values of around 50% [17]. The requirements for ore sorting vary from one case to another but it is common to impose a cut-off grade of around 0.2% [15].
From a mineral processing standpoint, the bigger the particles or rocks the less the chances of sulphide minerals from getting exposed to the environment. Such exposition is commonly associated with the concept of liberation. The liberation of a specific mineral was originally defined as the particle size threshold allowing the generation of particles composed of only one mineral [18]. From this definition, the liberation of each mineral present in an ore should be different as the presence of each mineral (or occurrence) changes from one to another. Such definition has been modified in time to better explain the efficiency of processes involved in metallurgy or mineral separation stages where the composition of the surfaces of particles is critical for their success [19]. For any geological occurrence of sulphide minerals (or any other mineral) the smaller the particle size the higher the liberation expected. The higher the liberation, the larger the exposure to the environment of surfaces containing such minerals and therefore the higher the chances of producing AMD. Nevertheless, there is in a way a trade-off between AMD flow rates and the potential of producing AMD.
Figure 3 shows two sets of particles having significant differences in particle diameter. The group of bigger particles will exhibit larger pore sizes although the air hold up may be similar for both case scenarios [20]. The set of particles exhibiting coarser sizes presents higher permeability than that of smaller sizes. Permeability depends on both static and dynamic properties of the porous medium and fluid characteristics. In the case of finer particles, capillary forces are more relevant which allow retaining more volume of the aqueous phase inside the porous material leaving the fluid phase and dissolved species to be transported slowly across through diffusive mechanisms favouring the acidification of the aqueous phase [21]. Coarser particles can produce higher flow rates reducing the residence time of fluid in contact with the surface of the particles. Then, there might be situations where the porous structure is fulfilled or saturated with water and the permeability can be modelled using the Darcy equation, however, for most case scenarios unsaturation would be frequently observed. So, permeability would be better modelled by the Soil-Water Critical Curve (SWCC) curve (Figure 4) which can be evaluated using three ranges of pressure values [Eqs. (3)–(5)] [22].
The impact of particle size distribution on mineral liberation and on permeability and its association with AMD generation.
SWCC Curve used to model the water content in an unsaturated porous media.
The parameters
The second section [Eq. (4)] located immediately to the right-hand side represents the behaviour of the porous media when the air gets inside displacing the water present in the pores which could correspond to an intermediate case observed in tailings where, by simple syneresis, the water drains across the material.
And the last section [Eq. (5)] represents the behaviour of the porous material when it gets dry leaving a certain residual water content, which describes a porous media where humidity is present mainly by wetting the surface of the particles.
Eq. (5) corresponds to later stages of tailings, the case of larger particles still retaining some water content (i.e., material coming from dump leaching or ore sorting operations) or abandoned tailings. From a thermodynamic standpoint, the suction is a function of the partial pressure of the pore-water vapour and the density of the vapour which depends on the temperature and can be computed as in Eq. (6).
And the permeability at residual water conditions can be computed from the matric (soil) suction as Eq. (7) [22].
One of the strong capabilities of Eq. (7) is that it correctly describes porous media with small particle sizes exhibiting lower permeability and higher water retention capacity [22, 23]. The latter would reduce the chances of producing large flow rates of AMD under these conditions [20]. Large flowrates would only then be possible in these conditions when water flows over the external surface of the piled-up porous material which reduces radically the exposed surface of the particles to the aqueous phase flowing around. Certainly, the magnitude of the drying conditions will depend on the water table present in each system. As it can be observed such description is based on semi-empirical mathematical models which is an indication that this is still a quite fruitful field of research.
Finally, the transport of liquid in porous materials built up of smaller particle sizes will expose the sulphide minerals in greater extension but they usually exhibit a higher hydrophobicity due to the presence of sulphur produced by oxidation reactions. This is known as natural hydrophobicity which occurs with much lower significance in the case of mineral oxides with stronger wettability properties. The liquid phase transferred through the porous medium needs to fill the voids displacing the air. Such subprocess is commonly referred to as imbibition and will be inhibited by the presence of sulphide hydrophobic surfaces which provide a first glance of how physics and chemistry are linked in these systems, but it is usually not considered. Indeed, physics and chemistry are frequently addressed by researchers separately. The relevancy of the chemistry and biology behind this process will be examined in the next subchapter.
There are several documents describing how sulphide minerals produce the so-called AMD, and the reader could refer to them for more information [4, 24]. Gas-solid and liquid-solid interactions are the major ones responsible for the significant differences between the chemical composition and structure of the bulk of the solid phase and the outmost surface layer arising from such interaction [25]. There are specific minerals that due to their instability under aerated conditions, notably metal sulphide minerals, are likely to produce enough acidity to stabilise several metals in dissolved state. Firstly, metal sulphide minerals would directly produce hydronium ions from their oxidation produced by the oxygen present in the atmosphere [Eq. (8)].
Such acidity is then enhanced by metal hydrolysis reactions occurring at the bulk of the aqueous phase. Hydrolysis can be represented by Eq. (9).
where the variable
Probably the most reported case study that exemplifies AMD generation is that of pyrite and marcasite (
In any case, the oxidation reaction is usually described as Eq. (10).
In Eq. (10) the oxidant, represented by the symbol
Electrochemical scheme of the I vs E curve presenting the most relevant electrochemical reactions as well as the mixed potentials.
Once ferric ions are formed in the aqueous phase, the oxidation rate of pyrite increases significantly not only because of the increase of the anodic overvoltage but also because of the high reversibility of the reduction reaction of ferric ions exhibits. Indeed, the mixed potential moves to higher voltages represented as (2) in Figure 5. Then, an accumulation of ferrous ions in solution may arise. The chances of regenerating the oxidant only by introducing oxygen would not be enough since the latter reaction still is mass transfer controlled. This is one of the most crucial issues the leaching of copper sulphide minerals presents which has been partially solved by microorganisms. In effect, it has been proved that bacteria, specifically,
Figure 6 summarises the main role of the two major types of bacteria,
Conceptual simplified model for generation of AMD.
Another more realistic analysis would involve coupling these two reactions. In this case, 2 mols of elemental sulphur would react with 3 mols of molecular oxygen producing 4 mols of hydronium ions and 2 mols of sulphate which is also troublesome for AMD (to be discussed in Section 5). Simultaneous oxidation of 12 mols of ferrous ions using 3 mols of molecular oxygen would then neutralise the acidity provided by the overall sulphur oxidation reaction by oxygen.
Supposedly, in real systems oxygen is slowly transferred to surface sites inside the porous media where the interaction with sulphide minerals exposed would produce elemental sulphur, one of the most relevant products generated at the surface of the particles, which then is oxidized due to the presence of microorganisms. Additionally, bacteria require oxygen and eventually carbon dioxide for growth, which is also responsible for producing both sulphur and acid [33]. It looks like the key would lie in inhibiting the formation of elemental sulphur which is quite insoluble (about
From all the above, it may infer that the chances of producing AMD cannot only be observed from a fluid dynamic or physical perspective. The gathering of key reactants needs to occur to produce it. Delays in the interaction between reactants given by the transport of oxygen, or carbon dioxide in less importance, will slow down the generation of acidity and therefore that of AMD.
It is precise because of this that many of the strategies to prevent AMD obey to block the reagents from coming into the porous material (Figure 7). For instance, with regards to the sulphide minerals present in the porous material authors have suggested removing it before piling up the solid wastes using froth flotation or any other selective separation method [36]. Bear in mind that this requires preparing the material for the separation process such as milling to certain particle diameter and the use of appropriate reagents at certain dosages to run froth flotation operations adequately. Another option would be to cover up only the surface of the particles exposing the sulphide mineral to the gaseous phase to avoid any contact with oxygen inhibiting the AMD formation [40]. A similar but more extensive blockage would entail forming a cap enclosing the whole porous material preventing oxygen from entering the system [41]. Even more, some researchers have suggested using materials known as not acid producers (or NAP) and directly carrying out some neutralisation of the AMD. It also has been suggested to introduce some positive pressure on inert gases to keep the oxygen from entering the system [42]. From the use of water, perhaps the most studied strategy for suspensions of mineral particles involves reducing the water content of slurries to dose lower amounts of neutralisation reagents [43]. And finally, with respect to the microorganisms, it has been recommended the use of some bactericides to prevent the acid-forming bacteria to appear in the system [44] while other authors have focused their attention in using some bacteria growth inhibitors [45].
Scheme of various strategies to prevent or treat AMD [
However, having implemented any of these paths to prevent AMD from appearing does not secure that it will not take place and if it occurs, several actions have been studied to deal with it. Furthermore, in many cases, these solid wastes are not appropriately disposed of over geomembranes or other impervious materials which forces continuously monitor surface- and ground-waters at the mining location outskirts. Whenever these waters acquire any properties resembling AMD, the wastewater treatment must act as a barrier to bringing the parameters of water quality back to their usual values. Even using such geomembranes does not ensure that the eventual AMD produced will be appropriately contained as the properties of these covers may also detrimentally evolve in time [56].
Mine closure is one of the subjects in the field of mine management that has gained notoriety over the last few decades [57]. The people´s perspective of mining activities is negative when abandoned mine sites impact adversely the environment or the nearby communities [58]. Figure 8A presents the iconic case of the Grand Canyon, in the United States, where mining activities were developed between 1957 to early 1960s. It can be observed that a section of the original plant is still in place and the exploitation has increased the surface area exposed to the atmosphere. In the same picture the before and after of a gold exploitation mine site located in the northern part of Chile shows a similar situation. In this case, the open-pit mine, unfortunately, made the entire town of
Pictures of two abandoned mine sites. (A.1 and A.2) Iconic case of Grand Canyon, United States, Guano Point, Bat Cave Guano Mine active between 1957 and early 1960, nowadays it is a renown National Park, (B.1) Before and (B.2) after gold mining exploitation of an open pit mine built at the heart of the small town
All mine sites have a definite lifetime. At the end of the mining exploitation, the site needs to be rehabilitated, ideally eluding any threat to the environment, or living organisms, vegetation, and nearby communities.
Behind this topic there are many concepts to address and it is difficult to summarise them in just a few lines. For instance, researchers have differentiated the terms mine closure and mine completion [59]. On one hand, mine closure is a procedure over a timespan where plant operation stops, and decommissioning is undertaken. On the other hand, mine completion refers to an aim of mine closure where the ownership is renounced by the mining lease and accepted by the next user of the land for a different purpose. These and other perspectives are still an ongoing theme for the whole society.
Despite the latter, for this quest to be successful, every government has stated a plan which considers not only technical requirements but also regulatory and legislation guidelines to prevent the sites to become hazardous reducing eventual further contamination in many years to come.
It was not necessary to go by a great deal of time before governments, mining companies and the whole society realised that the major threat behind the cease of a mining operation is the lack of planning. There are many reasons why mine sites close such as economics, geological, technical, regulatory, policy changes, social pressure, end of markets, etc. Therefore, it is not surprising that this stage of mine development requires a multidisciplinary set of actions. For instance, the actions relevant to the present subject might include:
Focused brainstorming aims at identifying environmental values, gains or losses inherent to AMD.
Preliminary evaluation of testing sulphide ore bodies for acid-based accounting and metals.
Potential use of overburden to cap potential generation of AMD.
As the Mine Closure conditions refer to the situation where the mining activities cease to take place, it is expected that energy, material, or personnel are not going to be available to deal with AMD. Therefore, unassisted wastewater treatment needs to be implemented.
The AMDs characteristics vary from site to site, however, for simplicity and without loss of generality the pH usually ranges between acid (close to pH 1 to 3) and slightly acid (around pH 5) which after wastewater treatment needs to reach pH values between 6.5 and 9 to be adequately discarded [60]. The acidity stabilises a concentration of certain heavy metals in aqueous solutions such as copper, zinc, chromium among others and metalloids like arsenic. Several physicochemical phenomena used to remove ions from an aqueous phase are succinctly reviewed in this section from both thermodynamic and kinetic classic modelling standpoints.
Perhaps this is the most straightforward strategy to treat AMD wastewaters coming from mine sites. The idea is to remove from the aqueous phase dissolved species that might be toxic to human beings and the environment by adding salts with high saturation or solubility product constant (
Sketch of the role of different ions formed during the dosing of quicklime to acidic aqueous solutions.
An initial concentration of metal is
The mathematical condition required for the precipitation to occur is given by Eq. (13).
Then, the efficiency of the treatment can be computed using Eq. (14).
The physical units of the different parameters in these equations need to be consistent. Plus, bear in mind that the efficiency of Eq. (15) is overestimated as only the major species were considered in this computation. Simultaneously, the precipitation of metals can be computed from Eq. (16). For the metal precipitation, Eq. (16) needs to be solved.
Eq. (16) does admit an analytical solution only in very specific conditions, so it is better to solve it numerically. Although it looks like this strategy is quite promising as it would be able to remove sulphate, heavy metals and even neutralise the acidic conditions of the AMD, it is somehow misleading for at least four reasons [63, 64]:
The precipitates being formed are not necessarily stable.
The dose of quicklime does not produce a perfect solution. It is most of the time leachate indicating that several particles are suspended and not instantaneously dissolved. This is to some point troublesome as the final pH will evolve in time reaching eventually much higher values.
Even more, such loss of control of pH may lead to an over increase of pH generating anionic species of the metals which will be redissolved increasing again their concentration in the aqueous solution. Even more, in many cases, the minimum concentration of heavy metals reached by using quicklime does not satisfy the maximum concentration permitted by current regulations.
Finally, there are many chances to get different quicklime dosing optimum points for metals and pH adjustment. Indeed, there are small chances that one single dosage of the reagent will exactly satisfy the minimum concentration of multiple heavy metals and the right pH at once. That is why this mechanism can only be used to approach best conditions for the correct discharge of the treated AMD.
During mine closure conditions this strategy is not directly recommended since the reagent dosing control is difficult to implement without personnel in place. However, the fundamentals behind this mechanism still hold. In the scenario of mine closure, the main idea would be to incorporate some sparingly soluble minerals with alkaline behaviour such as silicates, or others.
There are several studies focused on determining the dissolution rate of solids, especially that of quicklime in water. The first stage of dissolution is usually modelled by Eq. (17) [65].
where
The classic shrinking core model with reaction control can also be used (Eq. 18) [67, 68, 69].
where
This mechanism aims at removing pollutants from an aqueous phase by fixing them onto a surface of a solid which is stable when immersed in the wastewater. The adsorption mechanism is one of the preferred reactions for wastewater treatment not only because low-cost adsorbents consisting of by-products or wastes from other industries may be used, but also because it may reach high removing efficiencies of dissolved molecules with final concentrations of a few parts per billion [69]. Figure 10 presents several aspects to consider when picking up this mechanism. Different reactions between the adsorbent and the aqueous solution lead to the partial dissolution of the adsorbent affecting the local pH near its surface and its stability of the adsorbent suspension whenever forming small particles may occur [70].
Diagram of adsorption processes used in wastewater treatment.
There are several drawbacks behind the implementation of adsorption-based technologies. This technology requires optimising the contact between the solid phase and the aqueous phase containing the species to be adsorbed. Usually, piling up of adsorbent material in a column disposed of vertically or horizontally is preferred [71] but maintaining the permeability of the porous medium with time could become a challenge. It is also desirable to implement technologies using chemisorption rather than physisorption. Chemisorption has many advantages such as its specificity exemplified in Figure 10 by the single and double binding shown for the metal and sulphate. That is, different adsorption sites would be used by different types of adsorbates reducing the competition for adsorption sites. Plus, the relatively high binding energy associated with the adsorption process turns it quite irreversible from a kinetic standpoint which reduces the chances of pollutants desorption. Nevertheless, the main disadvantage would be that the eventual saturation of the adsorbent may be reached needing to move forward to a desorption stage to regenerate the adsorbent [72].
The thermodynamics of the adsorption process is explained in terms of the adsorption isotherm [73]. The adsorption isotherm is usually plotted in a graph where the y-axis represents the maximum quantity of adsorbed species per unit of the dry mass of adsorbent (also known as specific adsorption) while the x-axis presents the concentration of the species in equilibrium with the specific adsorption measured. All the data is obtained experimentally at a constant temperature and solids percent. There are many mathematical models that can be used to describe the process having each of the conditions and assumptions that as much as possible must represent the specifics of the process under study. The most used adsorption isotherms cited by researchers are the Langmuir and Freundlich isotherms as Eqs. (20) and (21) [74].
where
where
One general case to model adsorption kinetics is presented in Eq. (23) [75]
wherein the numerator there is a description of the classic law of mass action and in the denominator, the inhibition of the adsorption rate procured by the blockage of surface sites of other species in the system is incorporated. For example, the mathematical model for adsorption kinetics of one species labelled with the underscore “
where
This mechanism is highly valuable for certain ions which as product of the electron transfer type of reaction may directly precipitate or produce precursors for precipitation (Figure 11). The reduction of metals is somehow difficult to implement unless certain scrap of metallic wastes contain metals with low standard reduction potentials, also called less noble elements. If the metal is removed from the aqueous solution exhibits higher hydrolysis constants than the metal being released into the aqueous medium, the resulting pH of the solution should increase. One example of this would be the removal of polynuclear lead (II) ions by iron (II) ions [76, 77, 78].
Redox reactions in wastewater treatment.
The idea is to couple two electrochemical half-reactions, one half-reduction reaction and one half-oxidation reaction, having the former a higher standard reduction potential than the latter. As a requirement, since this wastewater treatment must occur without any energy input, the reaction must evolve spontaneously. Such a condition is presented in Eq. (25) [79].
Using Nernst equation, Eq. (25) would be of use to assess a first analysis of the impact of varying activities of different ions, partial pressures, or temperature on the spontaneity of the process can be assessed.
Electrochemical kinetics of spontaneous redox reactions are commonly studied in terms of the mixed potential theory and the corresponding current density. The mixed potential which is not a thermodynamic parameter is obtained from equalising the anodic and cathodic reactions [Eq. (26)]
In a complex system, there could be several reduction reactions and oxidation reactions occurring simultaneously in different locations within the system, therefore several mixed potentials may be installed. The open rest potentials, in this case, will attempt to follow such mixed potentials and depending on the conductivity of the species formed at the solid interface and at aqueous solution bulk such tracking down will be faster or slower [80].
This section is devoted to the design of AMD treatment systems which can operate in mine closure situations, close to stand-alone and unassisted systems to treat wastewaters. These treatment paths attempt to gather many of the mechanisms previously revised acting simultaneously to clean up AMD streams. Since most of these mechanisms need to take place spontaneously, many of these wastewater treatment systems attempt to mimic nature. Particularly, this subchapter addresses some aspects of two of these systems: Long-Term Permeable Reactive Barriers (LTPRB) and Horizontally Constructed Sub-Surface Wetlands (HCSSW).
On one hand, wetlands are one of the preferred passive wastewater treatment strategies to be implemented as a tertiary wastewater treatment [81]. Although it is considered a mature technology by many authors, it is one of the most difficult systems to model and understand. The latter is not only because of the many physicochemical interactions simultaneously taking place between all the species belonging to the system but also because of the multiple roles the local biota may play. For instance, sulphate ions are difficult to reduce using inorganic species only [82]. Indeed, looking at the Pourbaix diagrams, sulphate ions are stable over the whole pH range either in their acid form or not. It has been pointed out, though, that such reduction can be accomplished at the surface of organic material where carbon has a pivotal role. Indeed, it is well known that anaerobic systems, as well as aqueous media set in contact with solid metals, promote the growth of sulphate-reducing bacteria [83]. Carbon, among all its functions such as respiration, fermentation, methanogenesis, denitrification, and iron reduction would have a key role in sulphate reduction [84]. Sulphate reduction reactions are summarised by Eqs. (27), (28).
These reactions, though, are not in total agreement with classic electrochemical fundamentals. The standard electrode potential of the sulphate reduction is −220 mV vs SHE which is not fully consistent with the stability region of sulphate ions declared in Pourbaix diagrams [35]. Authors have indicated that such reduction is complex and involves metastable products [35, 85]. The reduction reaction would then consist of at least two reactions in series which are triggered by the sulphate activation by ATP sulphurylase increasing the potential to about −60 mV where the reduction from sulphate to sulphite is achieved. However, the reduction of sulphite to sulphide is yet not fully understood [86]. In addition, another disadvantage of these two reactions is, in principle, the production of carbon dioxide identified as a greenhouse gas. Additionally, authors have pointed out that the low performance in eliminating phosphorous may also be observed for other contaminants which usually increase the requirements in terms of residence time and/or surface lands available to implement these systems [87]. Whenever these systems are not available naturally, constructed wetlands are engineering-designed which can be implemented vertically or horizontally [84]. The latter corresponds to the case study to be described in the next section.
On the other hand, long-term permeable reactive barriers have captured interest from the scientific community since it houses several materials to treat wastewaters securing the correct quality of groundwater resources. The phenomena embedded in this type of strategy are mainly chemical or biological degradation, precipitation, and adsorption to immobilise contaminants [88]. Due to the similarities in dealing with organic matter between reactive barriers and wetlands, sulphate reduction bacteria can also be promoted in these systems. Additionally, the permeability of these systems needs to be secured. Unreactive or low-reaction alkali materials are used as a fixed bed introducing more reactive materials inside the pores that can range from specifically designed materials to wastes from other industries such as ferrihydrite-bearing soils or nanostructured calcium silicate adsorbent, among others [89, 90]. Since the growth of vegetation is not present in these systems, the permeability may be designed to avoid dead volumes or volumes with low mixing capabilities. Long term reaction kinetics is still a matter to do research on. Considering that a few reactions are associated to oxidation mechanisms by oxygen, and given the relatively low concentration of the gas, particularly in low permeability media, atmospheric corrosion perspective could improve the knowledge on these matters [91].
In a mine site located in the northern part of Chile, a pilot plant of AMD treatment designed by the company ISMP SpA consisting of LTPRB-HCSSW combined has been installed ideally to secure the water quality of surface waters for a timespan of a few years. It has been widely proved that different types of vegetation have absorption capabilities for different metals such as that shown in Figure 12 which corresponds to Phragmites Australis.
Picture of the AMD treatment pilot plant system implemented before being covered (a), and close-up to one of the Phragmites Australis used in the HCSSW (b).
The inlet pH was 5.0 and the aqueous solution flowrate is
with
Metal sulphide precipitation, though, is required to be formed as much as possible at pH values where hydrolysis of sulphide ions is low which could be accomplished by evaluating the competitiveness for sulphide complexation within the system. Otherwise, the acidification of the aqueous phase could again take place following Eq. (30).
Preliminary results indicate that LTPRB removes sulphate at between 10 and 30 times the rate reported for sulphate removal observed using wetlands only [92, 93]. The HCSSW allowed stabilising of the pH between 6 and 8. Preliminary computations indicate that the volume of control used is about one or two orders of magnitude lower than classic wastewater treatments. All these systems are complex by nature, but they could be engineering-designed from the beginning to enhance/inhibit reactions to avoid AMD. Now, considering the residence time of the AMD flowing through the system, is there any chance to adjust all these mechanisms to act standing alone at the appropriate rates enabling a wastewater treatment to last for a few years by itself keeping as much as possible the permeability of the porous media? This is certainly an opportunity still to be accomplished.
Acid Mine Drainage (AMD) formation is yet a process ill-understood. The AMD occurs spontaneously, and it is highly dependent on the local atmospheric conditions which makes it difficult to predict any of its characteristics. Preliminary strategies aiming at forming caps around these solid wastes could be considered a good first step towards preventing the formation of AMD. Nevertheless, in cases where AMD is already formed new strategies for isolating the wastes need to be considered.
Although the precursors of AMD such as sulphide minerals, and notably pyrite, water and oxygen are known to be involved, the physical chemistry and the biology linked to its production need to be studied in more detail and integrated, particularly in long-term reaction kinetics of the different mechanisms taking place.
Several strategies have been suggested to treat AMD. The condition of mine closure takes this challenge to the next level requiring a solution that cannot be intensive in the use of personnel, energy, or reagents.
Strategies involving passive wastewater treatment technologies which attempt to somehow mimic natural systems look promising.
Nowadays, the difference between passive and active wastewater treatment has become a thin line. On one hand, even passive wastewater treatment strategies require to some point the involvement of human resources. On other hand, new long-term permeable reactive barriers have been pointed out as wastewater treatment strategies than can gather several aspects of passive treatment systems such as low maintenance requirements to work and, simultaneously, exhibit fast wastewater treatment kinetics. Some practical aspects associated with implementing long-term permeable barriers coupled with constructed wetlands were presented but improvements with regard to the efficiency of these strategies to remove sulphate, heavy metals and other contaminants are still a matter of study.
Finally, perhaps the most relevant conclusion that can be drawn from this chapter is that addressing AMD generation, prevention or treatment is in fact a multidisciplinary topic where the conjunction of many specialities occurs such as chemistry, physics, hydrology, microbiology, electrochemistry, among others.
The author would like to dedicate and acknowledge the contribution to this study of Professor Fernando Valenzuela Lozano. For his invaluable friendship, his continued mentorship and all the technical and inspiring discussions across many years already, regarding hydrometallurgy and especially wastewater treatment of AMD. I would like to specially acknowledge the helpful input of Dr. Marcelo Sepulveda and Mr. Cesar Arredondo to this work. In addition, many thanks to Mr. Mario Solari and Mr. Thomas Ph. Chirino for providing pictures from industrial case scenarios and real-life portraits which had significantly increased the value of this manuscript. And, last but not least many thanks to Ms. Ana Maria Rojo for her assistance and good ideas to put together this chapter.
The author declares no conflict of interest.
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\\n\\nOpenness - We communicate honestly and transparently. We are open to constructive criticism and committed to learning from it.
\\n\\nDisruptiveness - We are eager for discovery, for new ideas and for progression. We approach our work with creativity and determination, with a clear vision that drives us forward. We look beyond today and strive for a better tomorrow.
\\n\\nIntechOpen is a dynamic, vibrant company, where exceptional people are achieving great things. We offer a creative, dedicated, committed, and passionate environment but never lose sight of the fact that science and discovery is exciting and rewarding. We constantly strive to ensure that members of our community can work, travel, meet world-renowned researchers and grow their own career and develop their own experiences.
\\n\\nIf this sounds like a place that you would like to work, whether you are at the beginning of your career or are an experienced professional, we invite you to drop us a line and tell us why you could be the right person for IntechOpen.
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Integrity - We are consistent and dependable, always striving for precision and accuracy in the true spirit of science.
\n\nOpenness - We communicate honestly and transparently. We are open to constructive criticism and committed to learning from it.
\n\nDisruptiveness - We are eager for discovery, for new ideas and for progression. We approach our work with creativity and determination, with a clear vision that drives us forward. We look beyond today and strive for a better tomorrow.
\n\nIntechOpen is a dynamic, vibrant company, where exceptional people are achieving great things. We offer a creative, dedicated, committed, and passionate environment but never lose sight of the fact that science and discovery is exciting and rewarding. We constantly strive to ensure that members of our community can work, travel, meet world-renowned researchers and grow their own career and develop their own experiences.
\n\nIf this sounds like a place that you would like to work, whether you are at the beginning of your career or are an experienced professional, we invite you to drop us a line and tell us why you could be the right person for IntechOpen.
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It has been argued that platforms provide reef-like habitat that increases the growth and survival rates of fishes by increasing prey availability and affording shelter for protection from predators, provide additional spawning substrate, and by acting as a visual attractant for organisms not otherwise dependent upon hard bottom. Platforms differ from most natural habitats, and from traditional artificial reefs, in that their vertical profile extends upward through the water column into the photic zone and the sea surface. Increased habitat quality on, or immediately around, oil and gas platforms are thought to be derived from increased in situ food production associated with encrustation by fouling organisms. In this chapter, we address the issue of how to evaluate the role of artificial reefs by first establishing levels of evaluation for individual fish species found on oil and gas platforms in the GOM. The levels of evaluation relate to the amount and adequacy of the available information, which was populated with an extensive literature and data search. Three levels of assessment are established, analogous to the levels of analysis established National Oceanographic and Atmospheric Administration (NOAA) Fisheries for identification of Essential Fish Habitat. More than 1300 documents, including reports, stock assessments, other gray literature, and papers published in the primary literature, were used to complete this chapter. When available, published literature was the preferred source of information.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"James H. Cowan and Kenneth A. Rose",authors:[{id:"139993",title:"Dr.",name:"James",middleName:"Howard",surname:"Cowan, Jr.",slug:"james-cowan-jr.",fullName:"James Cowan, Jr."}]},{id:"50363",doi:"10.5772/62876",title:"The Brown Seaweeds Fishery in Chile",slug:"the-brown-seaweeds-fishery-in-chile",totalDownloads:1716,totalCrossrefCites:4,totalDimensionsCites:10,abstract:"Chilean fishery of brown algae includes species belonging to the genus Lessonia, Durvillaea, and Macrocystis, which can be found along the coast, ranging latitudes from 18° to 55°S. The exploitation of these seaweeds is done mainly in the Northern coast because the environmental conditions of this region decrease initial production costs. Brown algae are exploited from natural populations and exported to international markets as row material, source of alginates, widely utilized in diverse manufacturing processes and industries. International demand for Chilean kelps has produced sustained increase in harvest during the last decade, reaching more than 390,000 dry tons/year. This chapter approaches the most relevant aspects of the brown seaweed fishery in Chile which covers a wide range of the Southeast Pacific coast, considering the number of commercial species, its abundance and distribution, knowledge achieved on their ecology and biology regarding management, and conservation of these resources, and finally, provides tools for stakeholders and policy makers directed to sustainable management of natural kelp beds occurring in the cold temperate seas.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Julio A. Vásquez",authors:[{id:"180745",title:"Dr.",name:"Julio",middleName:null,surname:"Vásquez",slug:"julio-vasquez",fullName:"Julio Vásquez"}]},{id:"56228",doi:"10.5772/intechopen.70028",title:"A Review of the Mitogenomic Phylogeny of the Chondrichthyes",slug:"a-review-of-the-mitogenomic-phylogeny-of-the-chondrichthyes",totalDownloads:1439,totalCrossrefCites:6,totalDimensionsCites:9,abstract:"The phylogenetic analysis of the Chondrichthyes has been the subject of intense debate over the past two decades. The principal relationships within the group based on the analysis of morphological traits are inconsistent with the available molecular topologies, and the phylogeny of these animals is highly controversial, at all levels, ranging from superorders to families and even the genera within families. With the recent development of new generation sequencing (NGS), many phylogenies are now being inferred based on the complete genome of the species. In 2015 and 2016 alone, around 21 new elasmobranch genomes were made available in GenBank. In this context, the principal objective of the present study was to infer the phylogeny of the sharks and rays based on the complete mitochondrial genomes available in the literature. A total of 73 mitogenomes of chondrichthyan species were analyzed. The phylogenetic trees generated rejected the “Hypnosqualea” hypothesis and confirmed the monophyly of the Neoselachii and Batoidea as sister groups of the sharks. These mitogenomic analyses provided ampler and more complete insights into the relationships between the sharks and rays, in particular, the topologies obtained by the analyses revealed a number of incongruities in certain groups of sharks and rays, and the interrelationships between them.",book:{id:"5895",slug:"chondrichthyes-multidisciplinary-approach",title:"Chondrichthyes",fullTitle:"Chondrichthyes - Multidisciplinary Approach"},signatures:"Divino Bruno da Cunha, Luis Fernando da Silva Rodrigues‐Filho and\nJoão Bráullio de Luna Sales",authors:[{id:"104512",title:"Dr.",name:"Luis Fernando",middleName:null,surname:"Rodrigues-Filho",slug:"luis-fernando-rodrigues-filho",fullName:"Luis Fernando Rodrigues-Filho"},{id:"205219",title:"Dr.",name:"Divino Bruno",middleName:null,surname:"Da Cunha",slug:"divino-bruno-da-cunha",fullName:"Divino Bruno Da Cunha"},{id:"205690",title:"Dr.",name:"João Bráullio De",middleName:null,surname:"Luna Sales",slug:"joao-braullio-de-luna-sales",fullName:"João Bráullio De Luna Sales"}]},{id:"55984",doi:"10.5772/intechopen.69471",title:"Deep-Water Sharks, Rays, and Chimaeras of Brazil",slug:"deep-water-sharks-rays-and-chimaeras-of-brazil",totalDownloads:1574,totalCrossrefCites:1,totalDimensionsCites:9,abstract:"The deep-water fishery in Brazil is currently in expansion due to depletion of most neritic economic species. This increasing deep-water effort brings concern on the bycatch impact, its specific composition, the need for capture’s evaluation and development of bycatch reduction devices. The impact is particularly aggressive on deep-water elasmobranchs, which have an extreme ecological k-strategy due to their reproductive constraints (lower fecundity and late first maturity age). Scientific deep-water surveys and intensive research programs (REVIZEE) along the past decade indicate that Brazilian elasmobranch diversity is higher than previously imagined. However, the deep-water fishery threatens this poorly known community of sharks and rays on the Brazilian continental slope as they become bycatch of a fast-growing and uncontrolled fishery. The recent study case of the monkfish (Lophius gastrophysus) fishery dynamics, well presented and discussed by the Brazilian scientific community, provided evidence of the need of bycatch-specific monitoring programs and fast-response fishery regulations. The present work discusses the Brazilian deep-water elasmobranch bycatch problem under the light of its biological diversity and completely unknown population status. Suggestions and management considerations are presented in order to coordinate and manage the establishment and growth of this deep-water fishery in Brazil.",book:{id:"5895",slug:"chondrichthyes-multidisciplinary-approach",title:"Chondrichthyes",fullTitle:"Chondrichthyes - Multidisciplinary Approach"},signatures:"Getulio Rincon, Rodrigo Cordeiro Mazzoleni, Ana Rita Onodera\nPalmeira and Rosangela Lessa",authors:[{id:"205621",title:"Dr.",name:"Getulio",middleName:null,surname:"Rincon",slug:"getulio-rincon",fullName:"Getulio Rincon"},{id:"206465",title:"MSc.",name:"Rodrigo",middleName:null,surname:"Mazzoleni",slug:"rodrigo-mazzoleni",fullName:"Rodrigo Mazzoleni"},{id:"206466",title:"MSc.",name:"Ana Rita",middleName:null,surname:"Palmeira",slug:"ana-rita-palmeira",fullName:"Ana Rita Palmeira"},{id:"206467",title:"Dr.",name:"Rosangela",middleName:null,surname:"Lessa",slug:"rosangela-lessa",fullName:"Rosangela Lessa"}]},{id:"52331",doi:"10.5772/64252",title:"Setting Up Traceability Tools for the Indonesian Blue Swimming Crab Fishery: A Case Study in Southeast Sulawesi",slug:"setting-up-traceability-tools-for-the-indonesian-blue-swimming-crab-fishery-a-case-study-in-southeas",totalDownloads:1665,totalCrossrefCites:2,totalDimensionsCites:5,abstract:"The Indonesian blue swimming crab fishery developed rapidly during the 1990s to become an important source of income for coastal communities. The blue swimming crab (BSC) in 2015 is the third highest export commodity in Indonesia, primarily to USA markets. Southeast (SE) Sulawesi is a relatively minor area for blue swimming crab production (approximately 1200–2000 mt per annum), in which only a subset of Asosiasi Pengelolaan Rajungan Indonesia (APRI) members are active, and it may be a conducive region in which to conduct a pilot activity to form a fisheries management structure that demonstrates the benefits that can be achieved via collaboration. The control document (CD) is a traceability and documentation process to be implemented by all of the segments of the supply chain (collectors/cooking stations, miniplants, and processors) in order to promote compliance to new Ministry and Marine Affair (MMAF) regulations and generate the records and documents of the supply chain application and verification of the new regulations. The self-recorded logbook by the fishermen and miniplant, as the point in the supply chain, could help with a meaningful and long-term solution to the fishery management in Southeast Sulawesi. This is the first trial of CD in Indonesia and could be a good model for BSC fishery in other region in Indonesia.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Hawis Madduppa, Zairion, Siti Nuraini, Kuncoro Nugroho and\nBambang Arif Nugraha",authors:[{id:"180161",title:"Dr.",name:"Hawis",middleName:null,surname:"Madduppa",slug:"hawis-madduppa",fullName:"Hawis Madduppa"},{id:"185944",title:"Dr.",name:"Zairion",middleName:null,surname:"Zairion",slug:"zairion-zairion",fullName:"Zairion Zairion"},{id:"185945",title:"Mrs.",name:"Siti",middleName:null,surname:"Nuraini",slug:"siti-nuraini",fullName:"Siti Nuraini"},{id:"185946",title:"Mr.",name:"Bambang Arif",middleName:null,surname:"Nugraha",slug:"bambang-arif-nugraha",fullName:"Bambang Arif Nugraha"},{id:"185947",title:"Mr.",name:"Kuncoro Catur",middleName:null,surname:"Nugroho",slug:"kuncoro-catur-nugroho",fullName:"Kuncoro Catur Nugroho"}]}],mostDownloadedChaptersLast30Days:[{id:"50289",title:"Effect of Special Fish Feed Prepared Using Food Industrial Waste on Labeo rohita",slug:"effect-of-special-fish-feed-prepared-using-food-industrial-waste-on-labeo-rohita",totalDownloads:2256,totalCrossrefCites:0,totalDimensionsCites:0,abstract:"All food processing industries generate wastes of varying nature in significant quantities. Managing these wastes so as to minimize the impact on the environment is the prime concern. The concept of waste has undergone much change in recent times, with the focus being on utilizing the waste materials as inputs for generation of new or reusable products. Vegetable and fruit wastes are generated in significant quantities and are easily available at minimal charge. The comparative utilization of these wastes as a dietary ingredient was assessed employing the Labeo rohita fingerlings as the test species. The study was conducted over a period of 60 days. Orange peels and potato peels are characterized, and then, formulation of orange peel feed (OPF) and potato peel feed (PPF) was carried out. Market common fish feed (CFF) was taken as a control. The three test diets were designated as CFF, OPF and PPF. Feeding was done once daily. The water quality parameters such as dissolved oxygen, water temperature pH, total alkalinity, total hardness; calcium hardness and magnesium hardness as well as growth response were monitored at fortnightly intervals. The quality of water was maintained by periodic partial replenishment over the period of study. On termination of the trial, higher growth response was recorded in the PPF treatment. The initial and final weight and length of fishes was recorded. The results shows significant growth in PPF and OPF showed brighter body scales than other two feed. Fishes were very healthy and normal throughout the study period indicating no adverse effect on their health. No infection whatsoever was noted during 60 days of experimental period.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Sanyogita R. Verma and Shanta Satyanarayan",authors:[{id:"183699",title:"Dr.",name:"Verma",middleName:"Rajroop",surname:"Sanyogita",slug:"verma-sanyogita",fullName:"Verma Sanyogita"},{id:"185353",title:"Dr.",name:"Shanta",middleName:null,surname:"Satyanarayan",slug:"shanta-satyanarayan",fullName:"Shanta Satyanarayan"}]},{id:"51124",title:"Fishery Status and Taxonomy of the Carangids (Pisces) in the Northern Arabian Sea Coast of Pakistan",slug:"fishery-status-and-taxonomy-of-the-carangids-pisces-in-the-northern-arabian-sea-coast-of-pakistan",totalDownloads:1927,totalCrossrefCites:0,totalDimensionsCites:0,abstract:"The objectives of this study were i) to evaluate number of existing members of the family Carangidae in the area ii) to establish a distinguishable and lucid key based on the taxonomic characteristics, meristic count and otolith description. In this study, thirty-six species were collected from the main fish landing facilities between 2012~2015. Fish body colour, taxonomic characteristics, fin rays and otolith shape description were used to identify each species. Otolith description comprises of shape of ostium, sulcus and margins of anterior and posterior surface along with distinct definite shape possess by each species make it easier for identification.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Nazia Qamar, Sher Khan Panhwar and Ghazala Siddiqui",authors:[{id:"182414",title:"Dr.",name:"Sher Khan",middleName:null,surname:"Panhwar",slug:"sher-khan-panhwar",fullName:"Sher Khan Panhwar"},{id:"184264",title:"Dr.",name:"Nazia",middleName:null,surname:"Qamar",slug:"nazia-qamar",fullName:"Nazia Qamar"},{id:"184265",title:"Prof.",name:"Ghazala",middleName:null,surname:"Siddiqui",slug:"ghazala-siddiqui",fullName:"Ghazala Siddiqui"}]},{id:"50583",title:"Trawl Selectivity in the Barents Sea Demersal Fishery",slug:"trawl-selectivity-in-the-barents-sea-demersal-fishery",totalDownloads:1672,totalCrossrefCites:1,totalDimensionsCites:1,abstract:"This chapter provides a general overview of the Barents Sea demersal trawl fishery. First, it reviews historical catch levels and current biomass status of four commercially important demersal species (cod, haddock, Greenland halibut, and redfish) and includes an overview of their management plan that has been carried out by the Joint Norwegian–Russian commission. Then, it presents the evolution of the technical regulations for improving size selectivity in this fishery and describes current challenges in gear selectivity. Later, this chapter describes the concept of size selectivity, introduces the selective parameters that define a selection curve, and progressively introduces different parametric models that describe the selection process. The most common experimental methods and gear used to collect selectivity data are described, and their advantages and disadvantages are discussed. Finally, this chapter describes an alternative, or a complementary method, to the conventional estimation of trawl selectivity—the FISHSELECT method. This method is based on morphology measurements and fish penetration models to estimate the selective properties of different mesh shapes and sizes at different mesh openings, which are later used to provide simulation-based prediction of size selectivity. FISHSELECT has already been applied to four important species of the Barents Sea Demersal Fishery, and the results have in all cases showed to be coherent with the results obtained from sea trial results.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Eduardo Grimaldo, Manu Sistiaga, Bent Herrmann and Roger B.\nLarsen",authors:[{id:"107079",title:"Dr.",name:"Eduardo",middleName:null,surname:"Grimaldo",slug:"eduardo-grimaldo",fullName:"Eduardo Grimaldo"},{id:"185311",title:"Dr.",name:"Manu",middleName:null,surname:"Sistiaga",slug:"manu-sistiaga",fullName:"Manu Sistiaga"},{id:"185312",title:"Dr.",name:"Bent",middleName:null,surname:"Herrmann",slug:"bent-herrmann",fullName:"Bent Herrmann"},{id:"185313",title:"Prof.",name:"Roger B.",middleName:null,surname:"Larsen",slug:"roger-b.-larsen",fullName:"Roger B. Larsen"}]},{id:"50363",title:"The Brown Seaweeds Fishery in Chile",slug:"the-brown-seaweeds-fishery-in-chile",totalDownloads:1716,totalCrossrefCites:4,totalDimensionsCites:10,abstract:"Chilean fishery of brown algae includes species belonging to the genus Lessonia, Durvillaea, and Macrocystis, which can be found along the coast, ranging latitudes from 18° to 55°S. The exploitation of these seaweeds is done mainly in the Northern coast because the environmental conditions of this region decrease initial production costs. Brown algae are exploited from natural populations and exported to international markets as row material, source of alginates, widely utilized in diverse manufacturing processes and industries. International demand for Chilean kelps has produced sustained increase in harvest during the last decade, reaching more than 390,000 dry tons/year. This chapter approaches the most relevant aspects of the brown seaweed fishery in Chile which covers a wide range of the Southeast Pacific coast, considering the number of commercial species, its abundance and distribution, knowledge achieved on their ecology and biology regarding management, and conservation of these resources, and finally, provides tools for stakeholders and policy makers directed to sustainable management of natural kelp beds occurring in the cold temperate seas.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Julio A. Vásquez",authors:[{id:"180745",title:"Dr.",name:"Julio",middleName:null,surname:"Vásquez",slug:"julio-vasquez",fullName:"Julio Vásquez"}]},{id:"50462",title:"Direction of Fisheries (SUISAN) Education from a Historical Perspective in Japan",slug:"direction-of-fisheries-suisan-education-from-a-historical-perspective-in-japan",totalDownloads:1400,totalCrossrefCites:0,totalDimensionsCites:0,abstract:"Fishing, aquaculture, and food processing is collectively referred to as “SUISAN”, and the term was translated to “fisheries” in the Meiji period. Fisheries education in Japan was at its dawn. Fisheries education was necessary for improvement of local fisheries subsistence. Fisheries education was performed, centering on nurturing of mid-career engineers for deep-sea fishing after 1950s. However, when the Heisei period in the 1990s started, “participatory = citizen involvement type fisheries education” was promoted extensively. Future establishment of a Japanese version of Sea Grants is desired to promote citizen involvement in fisheries education with systematized involvement of universities, research institutions, aquaria, and local people.",book:{id:"5210",slug:"fisheries-and-aquaculture-in-the-modern-world",title:"Fisheries and Aquaculture in the Modern World",fullTitle:"Fisheries and Aquaculture in the Modern World"},signatures:"Tsuyoshi Sasaki",authors:[{id:"180712",title:"Dr.",name:"Tsuyoshi",middleName:null,surname:"Sasaki",slug:"tsuyoshi-sasaki",fullName:"Tsuyoshi Sasaki"}]}],onlineFirstChaptersFilter:{topicId:"40",limit:6,offset:0},onlineFirstChaptersCollection:[],onlineFirstChaptersTotal:0},preDownload:{success:null,errors:{}},subscriptionForm:{success:null,errors:{}},aboutIntechopen:{},privacyPolicy:{},peerReviewing:{},howOpenAccessPublishingWithIntechopenWorks:{},sponsorshipBooks:{sponsorshipBooks:[],offset:0,limit:8,total:null},allSeries:{pteSeriesList:[{id:"14",title:"Artificial Intelligence",numberOfPublishedBooks:9,numberOfPublishedChapters:87,numberOfOpenTopics:6,numberOfUpcomingTopics:0,issn:"2633-1403",doi:"10.5772/intechopen.79920",isOpenForSubmission:!0},{id:"7",title:"Biomedical Engineering",numberOfPublishedBooks:12,numberOfPublishedChapters:98,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2631-5343",doi:"10.5772/intechopen.71985",isOpenForSubmission:!0}],lsSeriesList:[{id:"11",title:"Biochemistry",numberOfPublishedBooks:27,numberOfPublishedChapters:287,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2632-0983",doi:"10.5772/intechopen.72877",isOpenForSubmission:!0},{id:"25",title:"Environmental Sciences",numberOfPublishedBooks:1,numberOfPublishedChapters:9,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2754-6713",doi:"10.5772/intechopen.100362",isOpenForSubmission:!0},{id:"10",title:"Physiology",numberOfPublishedBooks:11,numberOfPublishedChapters:139,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2631-8261",doi:"10.5772/intechopen.72796",isOpenForSubmission:!0}],hsSeriesList:[{id:"3",title:"Dentistry",numberOfPublishedBooks:8,numberOfPublishedChapters:129,numberOfOpenTopics:0,numberOfUpcomingTopics:2,issn:"2631-6218",doi:"10.5772/intechopen.71199",isOpenForSubmission:!1},{id:"6",title:"Infectious Diseases",numberOfPublishedBooks:13,numberOfPublishedChapters:106,numberOfOpenTopics:3,numberOfUpcomingTopics:1,issn:"2631-6188",doi:"10.5772/intechopen.71852",isOpenForSubmission:!0},{id:"13",title:"Veterinary Medicine and Science",numberOfPublishedBooks:10,numberOfPublishedChapters:103,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2632-0517",doi:"10.5772/intechopen.73681",isOpenForSubmission:!0}],sshSeriesList:[{id:"22",title:"Business, Management and Economics",numberOfPublishedBooks:1,numberOfPublishedChapters:12,numberOfOpenTopics:2,numberOfUpcomingTopics:1,issn:null,doi:"10.5772/intechopen.100359",isOpenForSubmission:!0},{id:"23",title:"Education and Human Development",numberOfPublishedBooks:0,numberOfPublishedChapters:0,numberOfOpenTopics:2,numberOfUpcomingTopics:0,issn:null,doi:"10.5772/intechopen.100360",isOpenForSubmission:!1},{id:"24",title:"Sustainable Development",numberOfPublishedBooks:0,numberOfPublishedChapters:9,numberOfOpenTopics:4,numberOfUpcomingTopics:1,issn:null,doi:"10.5772/intechopen.100361",isOpenForSubmission:!0}],testimonialsList:[{id:"13",text:"The collaboration with and support of the technical staff of IntechOpen is fantastic. 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