Search Documents

By Jilai Xue, Jun Zhu, Liang Liu

"Separation removal of fluorite and calcite from scheelite is a difficult technical operation in current industrial practice with a heating process causing large energy consumption and high production costs. In this work, the floatation separation at room temperature were carried out using two types of skarn scheelite ores. The results showed that CaO and Na203 are better than NaOH as a regulator in pH value. In the rough floatation and first cleaning floatation, CaO (500g/t), Na203 (3000g/t) were used as a pH regulator, waterglass (4000g/t) was as a gangue depressant, oleic acid or sodium oleate were used as a collector. The degree of the obtained W03 concentrate was more than 65% (commercial product).IntroductionThe mainly gangue in scheelite are quartz, calcite, barite and some rare metal ores. There are three main types of scheelite for floatation: scheelite--quartz (silicate minerals) type, scheelite-calcite/ fluorite type, scheelite--calcite/fluorite/barite type. Generally speaking, scheelite--quartz type is separated easily, and others are difficult, on the contrary. The last two kinds of scheelite are always called scheelite--calcite/fluorite (barite) type, because there are similar floatation ability and floatation process between them. Scheelite, calcite and fluorite have same cation - Ca2+, it makes them have close floatation property [1]. Separation removal of fluorite and calcite from scheelite is a difficult technical operation in current industrial practice.The traditional separation method is a heating floatation process (Petrov's process) [2]. It can deal with many kinds of scheelite, and can be obtained stable quality ofW03 concentrate. On the other hand Petrov's process causes large energy consumption, high production costs and bad operational environments. Since 1980s, scheelite ambient temperature floatation has become the mainstream of study [3]. Nowadays more and more studies on scheelite floatation focus on complex reagent system [4, 5], rigid operating rules and at the same time development new regulator [1, 5]. Some research show there are new regulators can concentrate scheelite efficiently, but it may cause high costs, potential pollution and difficulty to spread. Oleic acid and sodium oleate used as collector have high adsorption capacity to scheelite, but same to calcite and fluorite[6]. So, it would not get ideal effect for separation of scheelite. In this work, the floatation separation at room temperature were carried out using two kinds of skarn scheelite ores. Calcium oxide and sodium carbonate was used as a pH value regulator, waterglass was used as a depressant and Oleic acid/sodium oleate was used as a collector. The result of experiment showed that the degree of the obtained W03 concentrate was more than 65% by one time ambient temperature roughing floatation, several times ambient temperature cleaning process."

Jan 1, 2014

By M. Oliazadeh, A. Vazirizadeh

"The inclusion of small amounts of silicon, phosphorus and sulphur in iron ores or concentrates can have a profound effect on the steel making process and thus on the final iron and steel products. In nature however, it is inevitable that iron deposits contain unwanted elements. Each element has its own distinct effect on the final steel product. The effect of high silicon is the formation of gray iron. Phosphorus mainly increases hardness and strength, lowers solidus temperature and increases fluidity and cold shortness. Finally sulphur contamination causes cracks in the iron texture when smelting and forms white iron when casting. Overall, the acceptable level of phosphorus, sulphur and silica in the iron concentrate should be less than 0.04%, 0.15 % and 1.5 % respectively.Scarcity of high grade iron ores necessitates using lower grade ores with higher amounts of impurities. The purpose of iron concentrators is to increase iron grades to an appropriate level suitable for steel making as well as removing impurities. Although many impurities can be traced in the ore, the most predominant impurities are limited to one or two elements. In this paper the beneficiation methods for removing SiO2, P and S are presented, including flotation, and the parameters that need to be considered in the design of beneficiation plants are discussed. Finally industrial cases are discussed along with their metallurgical performance.INTRODUCTIONIn metal sector, value of iron ores and concentrates is determined by iron percentage as well ascontent of:• Useful elements (Mn, Ni, Cr, V, Ti): natural alloying elements in steel• Deleterious impurities (S, P, As, Zn, Pb, K, Na): impair metal properties or complicate operational process in blast furnace• Fluxing components (Si, Ca, Mg,, Al)Sulphur and copper result in red-short, phosphorus is the cause of cold brittleness and arsenic and copper decrease welding characteristics. Sulphur should not exceed 0.15 in commercial ore. Acceptable sulphur content in ores and concentrates for producing sinter and pellets is 0.6%max, as sintering and heat hardening of pellets remove sulphur 60-90%. Phosphorous content in ores, sinter and pellets is limited to 0.07%-0.15%. 0.00.1% As max, 0.1-0.2% Zn max and up to 0.2% Cu are allowed in iron-ore part of the blast furnace burden for the production of standard conversion pig iron. Slag-forming components are divided into basic oxides (Ca, Mg) and acidic (Si, Al). Higher ratios of basic to acidic oxides are preferred since this reduces raw fluxing material."

Jan 1, 2016

The Golden Ridges Mine, one of the properties of New Guinea Goldfields Limited, is situated on the right bank of Nami Creek, not far from the township of Wau, in the Territory of New Guinea.The property is somewhat unique, in that the goldbearing ore-body occurs in the form of a flat seam-like deposit lying on a volcanic breccia, and covered with a mantle of overburden of decomposed porphyry. The overburden varies in thickness up to a maximum of about 65 ft.The ratio of overburden to ore is about 3 to 1. The practice developed is to strip the overburden by hydraulicking, and to mine the exposed ore under open-cut conditions, blasting to a vertical face, and using electrically operated scraper hoists for conveying the broken ore to the mill bins.The stripping of the overburden involves the boring of well-drill holes, blasting the holes and then hydraulicking the shattered material.

Jan 1, 1934

By J. P. Witherow

MR. BIRKINBINE'S description of the bad working and sudden chilling of the Warwick Furnace last summer, seems to me quite phenomenal in blast-furnace practice. During my connection with the management of blast furnaces for many years, in the anthracite, coke, and raw-bituminous coal districts, such a case has never come under my notice. It seems to me that the scaffold in the zone of fusion could not have established itself (so that the whole power of the engines, with a blast pressure ranging from 12 to 18 pounds per square inch, could not penetrate), unless the furnace was previously badly scaffolded and bridged in some of its upper sections, from 15 to 30 feet above the hearth level, either in the zone of chemical action or the beginning of the zone of fusion. Such a "barrier to the upward gaseous currents would cause a suspension of combustion which may have superinducedd the scaffold that is assumed to have existed in the zone of fusion. It is Difficult to conceive' that an agglomerated mass almost across the section of the lower bosh should have formed all at once, if the furnace was free and porous for the reaction of the gaseous currents above. Therefore, I think, the Warwick furnace was by no means in as free, open, and fine internal condition at the time the trouble commenced as the description of its regular working would lead us to suppose. I do not question the accuracy of the statements relative to the output of iron, etc. I merely claim that the phenomena., as described, could not have been almost instantaneously developed, unless there had been an incipient seaffold and lodgment above the zone of fusion. I would state my hypothesis to be that the stock lodged or collected in some of its upper sections during the process of blowing-in, on which, as a basis, more or less accumulations may .have lodged, and thus, indirectly, caused the formation of the suc- * This paper was not presented to the Institute in its present form, but is based on remarks, in discussion, by the author on Mr. Birkinbine's paper on, a Short Blast at the Warwick Furnace, and Mr. Witherbee's paper on Two Scaffolds at the Cedar Point Furnace.

Jan 1, 1881

Traditional in situ fan flow test methods under accepted standards require determinations to be made of both static pressures and total pressures during testing. This is to determine the resultant velocity pressures, which are vital in the accurate determination of the final fan airflow. These crucial velocity pressure (Vp) determinations are normally determined using simple manometric instrumentation such as an electronic manometer or an inclined liquid filled manometer. There is relatively little noise or fluctuation in the static pressure determinations and they can be quite easily and accurately recorded. There is almost always considerable fluctuation in the velocity pressure determinations though due to the highly turbulent and irregular velocity profile normally found in such in situ installations. This velocity turbulence means that the recording of such data is subject to random human error as the observer tries to average such fluctuations mentally during the observation period. Worse than this, and in the extreme, the recording of such velocity pressure data could actually easily be misreported if, for some reason, persons chose to do so.The author has devised a field method using highly accurate quartz crystal logging barometers to objectively record these velocity pressures. The method eliminates the ability to either mistakenly or intentionally misreport these crucial velocity pressures and is carried out in parallel with the recognised methodology, so result comparisons can be drawn. As such, a far greater level of confidence can be achieved in the final flow performance results than using the traditional more subjective method. Further to this it is difficult and almost impossible to refute the results using this ancillary substantiation method.The accurate determination of fan flows due to the impost of the carbon tax has taken on much more significance given the financial impacts in Australia at this time. The methodology detailed herein can be applied equally for both fan flow compliance testing and the verification of mine airflow data for greenhouse gas emission evaluations.The paper utilises the results of one 24-point pitot traverse to demonstrate the various findings. These include the very wide range of velocity pressures, which were logged at most of the measuring stations. It also illustrates how the method is utilised and compares the results derived from both this method and the more subjective traditional method along with the benefits of logging the velocity pressure results during the testing process.CITATION:Rowland, J A, 2013. Removing some subjectivity from traditional BS 848 and ISO 5802 in situ fan flow tests, in Proceedings The Australian Mine Ventilation Conference , pp 155-162 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Jul 1, 2013

By James S. Browning

This article describes research conducted by the University of Alabama's Mineral Resources Institute on removing sulfur from coal using a combination of gravity concentration and flotation methods. The research used the gravity and centrifugal force capabilities of Humphrey's spiral to remove part of the pyritic sulfur and ash. Flotation of the Humphrey's spiral coal concentrate removed additional sulfur and ash. In addition to obtaining good recoveries of high quality coal, the tests demonstrated that pyrite in the wastes could be isolated as enriched flotation products by the combined gravity-flotation approach. Domestic coal production in 1980 reached a record 757 Mt (835 million st). Forecasts are that coal production and use will approach 907 Mt (1 billion st) by 1985, with much of the increased production being used for electrical generation. Of current production, it is estimated that about 454 Mt (500 million st) of coal nationwide are subjected to some degree of cleaning, ranging from crushing and screening to gravity concentration and flotation. With expanded coal production and more rigid controls placed on coal combustion, it is reasonable to assume that the tonnage subjected to some form of preparation will increase, with time, thereby adding to the burden of coal rejects being generated. A major problem associated with increased coal use for electricity generation is the need for utilities to conform to emerging federal air quality standards for sulfur oxide emissions from power plants. To a lesser extent, other industrial operations burning coal face a similar situation. Controlling sulfur oxide emissions by using low-sulfur coal or resorting to stack gas desulfurization are two recognized approaches, but removing sulfur from the coal, if possible, by physical beneficiation before combustion is preferred because of its simplicity and lower cost. Reducing the inorganic sulfur in coal to tolerable limits by physical beneficiation, including flotation, as now practiced, is still relatively inefficient and has not kept pace with the more sophisticated physical beneficiation approaches generally employed by the nonfuel minerals industry. As one phase of a broad program conducted by the Mineral Resources Institute at the University of Alabama on sampling and evaluating impounded fine size waste coal, tests were made using samples from two impoundments to determine the quality of coal recoverable by a combination of Humphrey's spiral concentration and flotation. Particular attention was given to organic and inorganic sulfur deportment and distribution in the various products. Another objective was to determine if pyrite in the waste could be recovered for possible marketing. The use of Humphrey's spirals to concentrate fine coal was practiced as early as 1947. At that time, the Hudson Coal Co. used spirals to concentrate anthracite fines. In 1950, spirals were used to treat fine-size bituminous coal and later, in 1976, spirals were reportedly used for removing pyrite from fine-size coal. More recent investigations have discussed the use of Humphrey's spirals for treating fine-size waste coal in Alabama. Samples Description Washer waste samples were obtained from two impoundments. One sample was representative of waste generated during washing steam coal from the American, Pratt, and Nickel plate seams in Alabama. The other sample represented metallurgical coal washer waste from processing coal from the Carter, Johnson, and Milldale seams. Partial samples analyses are shown in Table 1, and screen analyses of the samples are given in Tables 2 and 3. Screen ana¬lyses showed that one sample contained about 4% of material coarser than 2 mm (10 mesh) and the other contained about 13% of plus 2 mm (10 mesh) material. Also, the analyses indicated that ash and sulfur increased as the material's particle size decreased. Experimental Laboratory Tests Sink and float tests using a heavy liquid (1.4 specific gravity) were made on the different screen sizes shown in Tables 2 and 3 to determine the effectiveness of gravity concentration for separating coal from pyrite and other gangue constituents. Tests indicated that gravity separation, under optimum conditions, could be expected to yield coal products containing 10-12% ash, and 0.2-0.3% pyritic sulfur. Good coal recoveries could also be expected. Using sink-float tests as a guide, tests were made in a Humphrey's spiral by a procedure in which a 90-135 kg (200-300 lb) portion of the

Jan 8, 1982

By M Cooper

Since its enactment in 1991, the Resource Management Act (RMA) has generated both praise and criticism. The major criticism is in relation to the costs the Act poses to industry and the time it takes to work through the process. In response to such criticisms the Minister for the Environment has initiated a review of the implementation of the RMA. The Minister's proposals for reform have not yet been released and the discussion that follows is based upon the report by the Minister's Review Group which was released in September.

Jan 1, 1998

By Charles H. McGuirk

The movement of iron ore, limestone and-coal on the great lakes involves an intricate transportation network between mine, dock, vessel, railroad and consumer. The system requires that stockpiling be performed at certain points in the pipeline because of the seasonal closing of the lakes, traditionally, this has been accomplished at origin and destination with a substantial cost. Impact to both the shipper and consumer, From the time that the raw material is removed from the ground, expeditious handling and movement to final destination is threatened by a series of potential delays. An initial movement from mine or processing plant to the upper lake port must be coordinated between rail equipment and dock facility, As each vessel is loaded, a schedule must be developed which routes the cargo to an unoccupied lower lake port. However, if the vessel is not delayed by unpredictable weather conditions on the lake, the boat may still arrive at a port congested with other vessels awaiting their turn to unload.

Jan 1, 1973

By André Alexandrino Lotto

A demanda global por energia renovável vem aumentando ao longo dos últimos anos. A energia solar é uma energia limpa e abundante, mas seu uso ainda é limitado por causa dos preços altos e baixa eficiência das células fotovoltaicas. O silício bruto, também chamado de silício de grau metalúrgico, tem sido alvo de muitos estudos visando sua purificação a um nível suficiente para aplicações de energia solar por processos mais baratos do que o processo convencional, chamado Processo Siemens. Neste trabalho, 3 kg de silício de grau metalúrgico foram fundidos por plasma térmico numa atmosfera de vapor de água, hidrogênio e argônio. O teor de boro foi reduzido de 10 ppm para 0,09 ppm em 18.000s (5 horas), mostrando que o processo poderia ser uma alternativa viável ao processo tradicional por via química

Aug 8, 2018

By Paula Aliprandini

Os minérios limoníticos de níquel apresentam na sua composição metais como ferro, níquel e cobalto, sendo o primeiro o elemento majoritário. A presença majoritária de ferro prejudica a separação dos demais metais que possuem interesse comercial. Para remoção do ferro, técnicas hidrometalúrgicas são usadas. A extração por solventes é uma técnica com foco na separação seletiva de metais. Neste trabalho, foi preparada uma solução sintética baseada nas concentrações dos metais presentes na lixiviação de um minério limonítico de níquel. A solução foi colocada em contato com o extratante Cyanex 272. Este extratante é conhecido pela sua seletividade ao ferro em valores de pH próximos a 2,0. As amostras foram analisadas utilizando a técnica de Espectroscopia de Fluorescência de Raios X por Energia Dispersiva (EDX). Após concluídos os ensaios foi encontrado que durante a extração do ferro, o cobalto foi coextraído junto, mesmo em pHs entre 0,5 e 2,0, indicando que a presença do ferro altera o comportamento do cobalto.

Aug 17, 2017

By Jocemir da Silva Santos, Alberto Vicente Belezia, Matheus Neves Lana

A regulação ambiental de processos industriais que geram efluentes contendo fluoretos é mundialmente restrita devido à alta toxicidade do íon. Na Ternium, a água de resfriamento recirculada no spray do Lingotamento Contínuo (WTP#2) dissolve parte do pó fluxante, resultando em concentrações de 20 a 30 mg/L de fluoreto. Para desenvolvimento do processo de tratamento de fluoreto que atendesse a legislação, mantendo no efluente tratado concentração de Fluoreto menor que 10mg/L e Alumínio menor que 3,0mg/L, foi realizada uma pesquisa utilizando um equipamento de Jar Teste convencional totalizando 165 ensaios. Os ensaios foram planejados segundo revisões bibliográficas descrevendo o método da precipitação química de fluoreto de cálcio, auxiliado por Cátions de Alumínio. Na conclusão da pesquisa, foi desenvolvida uma Rota Tecnológica para tratamento do efluente gerado na purga do sistema WTP#2 atendendo a legislação, atingindo uma remoção de 70% a 80% de Fluoreto. Ao final foi realizada uma etapa de otimização das dosagens, cujo resultado foi a redução do número de etapas de tratamento e uma redução na quantidade de produtos químicos utilizados, consequentemente reduzindo o custo de tratamento. A redução do custo de tratamento foi da ordem de 3 milhões de reais anuais, mantendo o efluente tratado com as concentrações dos contaminantes abaixo dos limites da regulação ambiental.

Aug 1, 2019

By Estéfano Aparecido Vieira

O presente trabalho busca desenvolver métodos de estudo de remoção de inclusões de aço em escala de laboratório relacionando propriedades como viscosidade e composição química das escórias com a capacidade de remoção de inclusões. Com esse fim, foram desenvolvidas cinco escórias usando como referência a viscosidade da fase líquida assim como o percentual da fase líquida. As escórias foram adicionadas sobre o aço fundido e comparou-se o nível de inclusões antes e depois dos experimentos. As escórias também foram analisadas após os experimentos através da difratometria de raios-x para identificação das fazes formadas. Os resultados apontam que as escórias testadas possuem a capacidade de remover inclusões. Porém escórias com elevado teor de CaO tem maior eficiência na remoção das inclusões.

Oct 30, 2017

By Gabriel Burlandy Mota de Melo

Manchas de óleo em um meio aquoso foram removidas utilizando compósitos de parafina com nanopartículas de ferritas de cobalto (CoFe2O4), níquel (NiFe2O4) e níquel-zinco (Ni0,7Zn0,3Fe2O4), nas proporções de 13,0% e 28,5% em peso. Para avaliar a eficiência da remoção, foi determinada a velocidade dos compósitos ao serem acoplados a uma mancha de óleo na superfície da água e submetidos ao campo magnético de um imã permanente. O melhor desempenho foi obtido com o compósito de parafina contendo 13,0% em peso de ferrita de níquel-zinco.

Aug 16, 2017

By Adelson Dias de Sousa

O objetivo deste trabalho é mostrar os estudos para remoção de sulfatos no efluentes industrial da Votorantim Metais Zinco, unidade Três Marias.Um dos maiores desafios na indústria que trabalha com meio sulfúrico em seus processos, é a remoção de sulfato de seus efluentes. Neste sentido a Votorantim avaliou vários processos distintos a fim de atingir uma concentração máxima de 250mg/L de sulfatos, dentre eles, precipitação química, redução biológica e resina de troca iônica.Dentre os processos avaliados, o que apresentou os melhores resultados foi a precipitação química através da formação de etringita, composto de fácil separação sólido-líquido, atingindo resultados de concentração de sulfato inferiores a meta máxima de concentração.

Aug 16, 2017

By Robert McClure, Carlton Lehman

Rendering safe explosives in an urban environment presents a unique challenge due to the safety concerns and disruption to the general public. Potential damage to the surrounding homes, businesses, utilities and transportation infrastructure are some of the major concerns when planning the render-safe operation. Engineering controls to mitigate blast effects, such as damaging air over pressure levels, material ejection and ground borne vibration, need to be implemented as part of the operation. Monitoring of seismic and air overpressure during these operations are needed to protect against potential claims when controlled or unplanned detonations occur. Two recent render-safe operations conducted in and around urban environments dealt with deteriorated, sensitive dynamite and damaged blasting caps. Utilizing innovative neutralization chemicals and processes to render-safe the deteriorated dynamite, while protecting the general public, proved to be the safest, most environmentally responsible and cost-effective way to approach the problem. In both cases, the explosives, old dynamite and detonators were found in abandoned, unlocked magazines. The dynamite was in a significantly deteriorated state, which was evident due to the nitroglycerine found leaking in,around and under the dynamite cartridges. Iron wire permissible electric blasting caps were also found in a corroded condition with exposed explosives and un-shunted lead wires. With occupied buildings within 180 feet (54.86 meters) of the magazines, any procedure (e.g. transporting, countercharging, burning) that could potentially cause a detonation was not an option. In the event of an unplanned detonation during neutralization operations, several blast mitigation methods were employed to safeguard the site. This operation and a similar one with over 1,000 pounds of crushed and buried leaky dynamite were unique since all the explosives were rendered-safe and neutralized on site. The use of advanced neutralization products and filtering processes allowed for a safer, more environmentally responsible way to resolve the problem. The magazines and all residual solids and fluids were tested and confirmed by independent labs to have no explosives residues. The effluents were treated on site, tested and met safe levels, so they were disposed of at a local municipal wastewater facility.

By Robert McClure, Carlton Lehman

Rendering safe explosives in an urban environment presents a unique challenge due to the safety concerns and disruption to the general public. Potential damage to the surrounding homes, businesses, utilities and transportation infrastructure are some of the major concerns when planning the render-safe operation. Engineering controls to mitigate blast effects, such as damaging air over pressure levels, material ejection and ground borne vibration, need to be implemented as part of the operation. Monitoring of seismic and air overpressure during these operations are needed to protect against potential claims when controlled or unplanned detonations occur.

Feb 1, 2020

By Bruno Rodrigues Henriques

O entendimento, controle e otimização do rendimento de aço líquido, em uma aciaria LD, é uma tarefa complexa e desafiadora. Qualquer projeto que se disponha a otimizar o rendimento de aço líquido irá se deparar com enormes dificuldades técnicas e operacionais. A despeito de todas as dificuldades e em função da importância do rendimento de aço líquido, uma vez que o mesmo tem forte impacto no custo de produção, toda aciaria procura manter essa variável de processo sob estrito controle. Esse trabalho se propõe a mostrar todas as etapas da condução de um projeto, desenvolvido e implantado em 2014, que tinha como foco entender, controlar e otimizar o rendimento de aço liquido. Durante o desenvolvimento do projeto, foi encontrado um total de 19 desvios e foram implementadas 23 ações corretivas. O valor do rendimento, que antes do projeto estava em torno de 91,6%, evoluiu para uma média de 93,5% em 2015 e 2016. Esse aumento de 1,9%, em média, no valor do rendimento de aço líquido, proporcionou uma expressiva redução no custo de produção na aciaria.

Aug 17, 2017

By Juan Daniel Martínez, Janaina Accordi Junkes, Dachamir Hotza, Tatiana Pineda

"The rice husk combustion in a bubbling and atmospheric fluidized bed reactor was investigated. The results showed the technical viability of producing both heat and amorphous silica from a renewable energy source. This paper presents the characterization of rice husk ash (RHA) obtained under varying fluidization velocities (0.13-0.15 m/s) and rice husk feed (4.5-7.2 kg/h). Characterization techniques include X-ray fluorescence, X-ray diffraction, particle size distribution and scanning electron microscopy. For the employed range of fluidization velocities of rice husk feed no noticeable influence on the chemical composition of produced RHA was observed. After combustion, RHA containing ~93% amorphous silica and <3% unburned char was obtained. RHA primary particles presented sizes from 90 to 100 µm and a tendency for agglomeration in aqueous media. Thus, the potential of this type of reactors with respect to speed, continuity and self-sufficiency energy of the process was shown.IntroductionDue to the increase of the agroindustrial production, the concern with processing by-products, such as rice husk (RH), is growing. For a better material and energy use, allowing a cleaner production and a more maintainable development, RH can be used as renewable fuel in the production plant, for instance, in steam generators. The adequate combustion of RH generates hot gases with low levels of pollutants, as carbon monoxide and particulate material.RH is the protecting coating formed during the growth of the rice grain, composed by four structural layers.1 The main components of the husk are cellulose and hemicelulose (50%) besides lignine (26%) and organic components (4%), as oils and proteins. The remaining amount includes inorganic materials (SiO2, Al2O3, K2O, Na2O, MgO, CaO, Fe2O3, MnO, P2O5).1The rice husk ash (RHA) is the product of the termochemical transformation of RH. The conditions of the different conversion processes (pyrolysis, gasification and/or combustion) determine the physical-chemical characteristics of the final product. RHA corresponds to 14 to 25% RH, depending on the variety of the rice, climate and soil of the producing area.2-4 The main component of RHA, which is generated at moderate combustion temperatures, is amorphous silica (SiO2) in the range from 80 to 97%.4,5"

Jan 1, 2008

By George Carico

Research and related demonstration projects are being conducted in West Virginia on both existing and former coal surface mine lands to determine potential post-mine land re-use options that offer the greatest likelihood of future benefit and success. Examples of projects include renewable energy considerations that incorporate solar, wind, and/or biomass options, and contain components designed to educate business, government entities and the local community on renewable energy options and potential opportunities Multiple property re-use options are being researched and evaluated, based on site-specific conditions and characteristics, including infrastructure, local community needs and regional economic conditions. Re-use options being explored include innovative uses and needs, such as specialty housing, unique business and industrial needs, and an extensive variety of recreational and small business opportunities that best fit the specific needs of the local community and regional economic structure.

Aug 1, 2013

By J. Bakos

Solar Hydrogen Energy Corporation (SHEC Labs) recently constructed a pilot-plant to demonstrate a Dry Fuel Hydrogen Generation System that is powered primarily by sunlight focusing-mirrors. The pilot-plant consists of: A Solar Mirror Array and Advanced Solar Concentrator and Shutter System; and two thermo-catalytic reactors to convert Methane, Carbon Dioxide, and Water into Hydrogen. Results from the pilot study show that Solar Hydrogen generation is feasible and cost-competitive with traditional Hydrogen production. More than 95% of Hydrogen commercially produced today is by the Steam Methane Reformation (SMR) of natural gas, a process that liberates Carbon Dioxide to the atmosphere. The SMR process provides a net energy loss of 30 to 35% when converting from Methane to Hydrogen. Solar Hydrogen production provides a 14% net energy gain when converting Methane into Hydrogen since the energy used to drive the process is from the sun. The environmental benefits of generating Hydrogen using renewable energy include significant greenhouse gas and criteria air contaminant reductions.

Jan 1, 2005