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By Isrun Bohlinger

Resources recovery of brasses for semifinished products often results in the formation of hard spots impairing the quality of following abrasive and/or surface finishing processes. A short survey is given on the recycling processes, followed by the actual knowlegde of genesis, composition, and possibilities of avoidance of hard spots. Informations on genesis and composition of hard spots are completed by data from recent experiments.

Jan 1, 1998

By Wellington Fernandes Junior

O uso de blocos de solo-cimento é considerado um método construtivo mais barato do que o convencional, visto que uma das matérias-primas, o solo, é abundante. Soma-se a isto, o fato de não haver uma destinação correta para o resíduo proveniente da fabricação de papel. Visando redução de custo de produção de tijolos de solo-cimento e uma alternativa sustentável para aproveitamento do resíduo, a proposta do presente trabalho é avaliar a incorporação do resíduo da fabricação de papel na mistura solo-cimento para confecção de tijolos modulares prensados com dimensões de 30cmx15cmx7cm. Foram testadas diferentes proporções de solo e resíduo e mantendo sempre a mesma massa de cimento. Foram realizados ensaios de absorção de água e resistência à compressão aos 28 dias de cura. Os resultados foram analisados a fim de verificar a viabilidade da incorporação do resíduo nos tijolos em maior quantidade possível, obedecendo as exigências impostas pelas normas regulamentadoras de blocos de solo-cimento. Foi concluído que a incorporação do resíduo, em quantidades adequadas, é viável na produção de tijolos de solo-cimento, reduzindo o custo da produção, além de diminuir os impactos ambientais com o destino correto do resíduo.

Oct 30, 2017

By K. Cybulski

Coal dust explosions still remain the main hazard in the coal mining sector, notwithstanding their relatively wide recognition compared to other hazards and the development of effective methods of prevention. Coal dust explosions are still the cause of numerous catastrophes, often leading to fatalities. Fortunately, they rarely occur, and it is for this reason that their hazardous impact is often underestimated. This problem in Poland is being exclusively solved by the Central Mining Institute, Experimental Mine Barbara. Here, basic research on the phenomenon of coal dust explosions and prevention methods is carried out, as well as investigations into the causes and circumstances of past accidents. After 15 years of no coal dust explosion accidents in Poland (1987?2002), a few coal dust explosions have recently occurred, with tragic consequences. These events have taken place not only in hard coal mines, where the presence of dangerous coal dust is the result of common production cycle, and safety measures against coal dust explosions are subject to specific regulations, but also in coal-fired power plants. This is of special concern because prior to 1987, such accidents had been been reported only for coal mines and not for coal-fired power plants. In recent years, two dust explosions occurred in Polish power facilities: the Dolna Odra and Turow power plants. In both cases, coal dust explosions occurred in the fuel supply system, but biomass dust was also involved. The explosions caused significant damage to the systems and buildings. This paper gives description and schematics of the regions of catastrophic coal dust explosions that have occurred in recent years in Poland, as well as the results of post-accident investigations, presenting the coal dust explosion hazard at the accident scene The results specify in detail the state of safety measures against coal dust explosions in light of the relevant regulations in force, including amount of deposited coal dust, content of incombustible matter in coal dust, free moisture content in coal dust, state of coal dust explosion safety zones, and state of explosion barriers. The conclusions from the site inspection and post-accident investigations presented enable us to determine locations of explosion initiation, probable ignition sources, range of explosion flames, and explosion barrier performance. A complete elimination of coal dust explosion hazard at the site of dust deposition is practically impossible to achieve. Similarly, a total elimination of ignition source, which may be related to the occurrence of other natural hazards, equipment malfunction or human errors, is impossible. The examples of tragic events that took place in Polish coal mines and coal-fired power plants highlight shortcomings and mistakes made in terms of assessment and prevention measures taken against the coal dust explosion hazard.

Aug 1, 2013

By Gerald H. Luttrell, Seyed Hassan Amini, Aaron Noble

One of the most important processing engineering tools for designing mineral processing facilities is linear circuit analysis. This technique, originally conceived and developed by Meloy, Williams, and Fuerstenau nearly four decades ago, provides fundamental insights regarding how unit operations interact and respond when arranged in multi-stage processing circuits. Researchers have successfully utilized this tool to improve the operating performance of industrial processing circuits incorporating coal spirals, magnetic separators, mineral spirals, and eddy current separators. More recently, advanced versions of this tool have also been developed to provide a standardized framework for circuit mass balance calculations, to output exact analytical solutions to mass yield and value-based efficiency expressions, and to estimate uncertainty propagation in separation circuits. This article reviews the historical development of linear circuit analysis, describes how the technique has evolved to address more complex circuit design problems, and presents industrial case studies that highlight the importance of this process engineering tool.

By E. C. Payne

"IntroductionTHE SMALLER industrial and commercial steam generating plants in the United States are suffering from an ‘engineering deficiency' which, if allowed to continue, will probably result in the extinction of the species• that now burn •approximately 75 million tons of coal. We will classify as 'small' those plants which should require not more than one operating man per shift, including those in which as little .as thirty minutes per day should be adequate for .all service attention. These are the small steam plants that need the most, and get the least, expert attention for fuel :planning, equipment selection, design layout, .and proper operating technique. Dissatisfaction with bituminous coal is usually caused by one or more preventable weaknesses such as excessive or burdensome labour •for firing, .coal or ash handling and manual operation, smoke and fly ash emission above nuisance levels:, high maintenance and premium coal application for acceptable operation, and .finally, overall steam costs which are not .competitive. These 'deficiencies', so .common in the small coal-fired steam plants, can be readily eliminated by competent engineering and modern equipment with automatic controls."

Jan 1, 1953

By H. M. Cooper

The determination of moisture in coal is an empirical test, because the time, temperature, and equipment are specified. The essential features of the equipment and details of the procedure are given in A.S.T.M. Designation: D271-44.:2. According to the specifications, the following features should be incorporated in the equipment used: 1. Oven must have uniform temperature in all parts. 2. Oven must be constructed with minimum of air space. 3. Oven must have means of changing the air two to four times per minute. 4. Air must be dried over sulfuric acid (sp. f-7. 1.84). The analytical procedures governing most of the nation's coal purchases are those given in A.S.T.M. Standards referred to above. These standards are general arid of such scope as to cover all ranks and types of coal. In cases where only the moisture is required, a faster method than the standard procedure is desired.

Jan 1, 1948

By Mory M. Ghomshei

"The cost of deep underground mine cooling depends on a number of geological, environmental and economic factors such as the temperature gradient in the mine, the outside air temperature, and the local price of energy. While geological factors, being static, can be controlled to some extent during the mine design, the environmental and economic factors dynamically change and therefore can only be controlled through a flexible mine ventilation system.With an average temperature gradient of 20–25°C/km, the virgin rock temperature at 2,000 m can reach 45–60°C. Conventional cooling at such depths could lead to exorbitantly high costs. In-mine geothermal heat pumps can considerably reduce the cost of cooling through energy communication with the centralized absorption chillers, which service the mine from the surface.It is shown that in-mine heat pump systems can be a viable option for reducing operating expenses and providing some degree of flexibility to cope with fluctuating energy costs. The price of Natural gas and electrify are the most important variables for optimizing the level of interaction between the surface and inmine cooling systems. Deep mine waters can be used to carry a portion of the mine heat to the surface, where the heat from mine can be used as a supplementary energy source for absorption chillers. As an extra benefit, the heat output of the chillers can be used for district heating and or greenhouse growing.The case of cooling deep levels of deep mines in Sudbury Canada (e.g. Creighton Mine) has been discussed. It is shown that an initial 1MW in-mine geothermal heat pump system can save significantly on the cost of cooling. Such a demonstration project will allow R&D on viability of larger similar systems to be incrementally added in the future.INTRODUCTIONThe amount of heat generated in deep and ultra-deep mines depend primarily on the regional temperature gradient and the thermal conductivity of mine rocks. The conductive heat flow is quantifiable and can be minimized or optimized in the process of mine design. Another important heat source can be related to underground equipment such as diesel machinery which often have low efficiencies (approximately 25–35%). This heat source can be controlled and reduced though improving efficiencies or using electrical equipment, which offer a much better efficiency (approximately 80–90%). Mine waters can also be a significant heat source (convectively bringing large amounts of heat into the mine workings)."

Jan 1, 2019

By William E. Saegart

Copper has been mined in the Philippines since at least as early as the Ming dynasty (1368 A.D. to 1644 A. D.). The principal source areas of this early production were in Camarines Norte (Paracale), in the Mountain Province, which now boasts the largest number of Philippine porphyry copper deposits, in Masbate and in Surigao, The Spanish Era began in 1521. Although they were primarily interested in gold, the Spaniards operated several copper mines including the San Remigio mine on Panay and the Lepanto mine in northern Luzon, beginning in 1842 and 1865 respectively. Prior to World War II most of the Philippine copper production was supplied by these same two mines together with the Hixbar mine, Rapu Rapu Island which began operation in 1939. The Hixbar and San Remigio mines are cupriferous pyrite deposits and the Lepanto is a vein-¬form replacement deposit (Kinkel et al. ,I 1956). No significant copper production was derived from porphyry copper occurrences prior to world War II.

Jan 1, 1976

By G. L. Anderson

The U.S. Bureau of Mines (USBM) has conducted research to improve the nondestructive testing (NDT) of wire hoist ropes. Losses in the diameter of a wire hoist rope are used as one criterion for judging when a rope should be replaced. Losses are determined by periodically measuring the rope diameter and comparing this measurement with the original measured diameter; when the diameter reaches a specified minimum at any point along its length, the rope must be retired. Generally, these measurements are made at randomly selected locations along the length of the rope, using a hand caliper. To provide more accurate measurements and to allow measurements to be taken continuously along the length of a hoist rope, an optical diameter-monitoring system was built for the USBM under contract. Continuous measurements are preferable because, when combined with continuous electro-magnetic NDT results, they can indicate whether losses in metallic cross-sectional area originate from external wear or internal wear and corrosion. Tests of the system showed that the instrument met specifications when measuring wire rope at low rope speeds but was inaccurate at speeds over about 30 m/min (100 ft/min). This report describes the prototype system, presents the results of the test program, and describes the capabilities of the system.

Jan 1, 2010

By Hajime Miki, Gde Pandhe Wisnu Suyantara, Tsuyoshi Hirajima, A. M. Elmahdy, Keiko Sasaki

"Seawater has been reported to depress molybdenite in a copper-molybdenum (Cu-Mo) flotation process at high pH due to the precipitation of Mg(OH)2. Meanwhile, to improve mineral recoveries, collectors are usually added into the flotation cells, thus adding the complexity to the mechanism of bubble-particle interactions involved in Cu-Mo flotation. Therefore, understanding the interaction mechanism in seawater flotation and in the presence of collectors is important to explain the minerals depression. The present work investigated the effect of kerosene on the bubble collision and attachment to pure chalcopyrite and molybdenite surfaces in MgCl2 solution as one of the seawater major components at pH 6 and 11. Mineral surfaces were characterized using atomic force microscopy (AFM). In addition, minerals floatability in the same system were tested in a column flotation. The study of bubble-particle interactions shows that following several collisions, bubble could displace the intervening liquid layer on the mineral surfaces, forming a three-phase contact (TPC). A TPC formed more rapidly in the presence of emulsified kerosene in a 0.01 M MgCl2 solution at pH 6 for both minerals. The reason is kerosene increased the surfaces hydrophobicity and destabilized the intervening liquid layer on the surfaces. Moreover, the average time required to form a TPC was shorter on molybdenite surface. This can be attributed to the effect of adsorbed kerosene on molybdenite surface and molybdenite surface roughness.INTRODUCTIONIn froth flotation, bubbles are used to separate hydrophobic mineral particles from hydrophilic particles. In this process, bubble-particle interactions (i.e., collisions, attachment, and detachment) are crucial with regard to mineral recoveries. The effectiveness of froth flotation depends on the formation of stable aggregates between the hydrophobic particles and the bubbles, allowing the bubble to carry the particles to the froth layer. To form such aggregates, the bubbles and particles must collide, and the intervening liquid layer must be drained below the liquid layer critical thickness, forming a stable threephase contact (TPC) (Ralston & Dukhin, 1999). Particles detachment may take place if the particles still have sufficient kinetic energy and the TPC is not formed. Previous studies of bubble-particle interaction in electrolyte solutions have been conducted using atomic force microscopy (AFM) (Assemi, Nguyen, & Miller, 2008), and by approaching the bubble using mica plate (Pushkarova & Horn, 2008), however, these studies did not focus on the bubble-particle collisions. Bubble collisions and attachment to hydrophobic (Teflon) and hydrophilic (glass) surfaces in a a-terpineol solution have been investigated by Krasowka et al. (2003)."

Jan 1, 2016

By Altair Lúcio de Souza

A laminação de tiras a quente com laminadores Steckel tem como característica um perfil de temperatura mais baixa nas pontas sendo este um dos motivos que geram cargas de laminação muito mais altas nesta região. A carga de laminação elevada tem como consequência no processo a geração de desvios de planicidade e o alto risco de rompimento do material nos passes finais de laminação. Este trabalho tem como objetivo demonstrar os benefícios da utilização da estratégia de Tapering para a laminação de tiras de espessura fina em laminador Steckel. Foi feita a comparação das cargas de laminação do material laminado e o acompanhamento dos resultados de planicidade obtidos antes e depois da implantação desta função. Ao fim do trabalho verificamos que a estratégia de Tapering é essencial para o processamento de materiais finos com laminadores Steckel.

Jul 30, 2018

The sixth Annual RMCMI Mine Rescue Evaluation was held during the 1997 Institute convention at Sheraton Steamboat Resort, Colorado. The Mine Rescue committee, co-chaired by Becki Boam and Gary Cook, is one of 18 committees of the Institute. In 1997 the largest number of teams participated in the program. There were nine: BHP Minerals - La Plata Mine, BHP Minerals - Navajo Coal Co., BHP Minerals - San Juan Coal Co., Bridger Coal Co., The Coteau Properties Co., General Chemical Co., The Sabine Mining Co., Solvay Minerals and Western Energy Co. Professional evaluators who provided challenging scenarios for the 80 participants were Jack Knight of Milton, Florida; Wilson Begay, Chris Saxon, and Gaylon Yazzie all of Western States Security; Mary Bailey, Bailey Associates; Tom Bass, California Department of Corrections; and Art Saenz, BDC. Seven members made up each team plus one or more trainers and represented the states of Montana, New Mexico, North Dakota, Texas and Wyoming. Ten different scenarios were presented during the two day evaluation. Each team was given the pertinent information to solve the problem as they assembled at the site. Mine Rescue families and friends participated as victims providing realistic scenarios to simulate the stress of an actual rescue incident. Each team was unaware of the circumstances until arriving at the various scenes in and around the Sheraton resort. [ ] These teams are providers of prompt rescue and medical care for accident victims at their respective properties. The members act with immediate and professional knowledge to save lives and prevent further injuries. Sponsors who contributed financially to the 1997 program are: Argo Industrial, Antelope Construction, Fisher Safety Supply, Flanders Electric Motor Service, Inc; Intermountain Electronics, Inc.; King Energy Services, Inc.; Rocky Mountain Electric Motors, LS.; TerraMatrix and Triune Inc. On Saturday evening, June 28, a reception was held for all mine rescue participants and spouses who had advance registered for this social event. The RMCMI Board of Directors was invited to attend and meet with the teams. As convention attendees, all mine rescue participants and registered families attended the Monday night country western reception and Bar-B-Q. This was followed by an adult western melodrama. [ ] Glass awards with the RMCMI logo and a Mine Rescue figure were presented at the Tuesday Mine Rescue buffet breakfast to all nine teams, each of which had achieved proficiency at level 3. Captains of the teams pictured below are (from left standing): Ron Neff, BHP-San Juan; Ted Laughline, Bridger, Terry Davis, Coteau; Jim Knutson, General Chemical (from left kneeling): Dan Allerdings, Rosebud; Ron Miller, BHP-Navajo; Jonathan Sorrell, BHP-La Plata and Ray Blaisdell, Solvay. Gary Cook is to be commended for his solo last minute supervision of the Mine Rescue program, due to Becki Beam's unavoidable absence. The teams look forward to the 1998 convention at Snowmass Village Resort, Colorado Thursday and Friday, June 25 and 26.

Jan 1, 1997

By F. S. White, E. L. Kinsella

THE solids fluidization process brought out by the Standard Oil Development Co. in the early forties for catalytic cracking of petroleum enabled rapid transfer of large quantities of heat from gases to solids under closely controlled temperature conditions. As the technique developed, it was natural that applications for the process outside the petroleum industry would be sought. The calcination of limestone to ' quicklime requires the transfer of a large quantity of heat at high and closely controlled temperatures. For these reasons, this possible application was one of the first to be investigated. Laboratory work conducted by the Dorr Co. indicated that lime produced by solids fluidization would be of exceptional quality. Calculation of theoretical heat balances showed that savings in fuel could be expected. Accordingly, a pilot plant of 10 tons per day capacity was erected by the New England Lime Co. at Adams, Mass., to substantiate the process. Operation of the pilot plant, previously described,1 showed that excellent lime could be produced with a saving in fuel. The work also indicated the necessity of preparing feed to remove the finer fractions if dust losses were to be held to a tolerable level. A single-stage fluidized solids drier-stripper was developed to accomplish this sizing.2 Subsequently a commercial lime reactor was erected at Adams, beginning operation in June 1949, followed by air sizer facilities completed in November 1951. This paper will describe these two applications of solids fluidization. The raw material for preparation of lime by the fluidizing process is a high calcium crystalline lime stone having the approximate chemical composition shown in Table I. The stone is first prepared by crushing and grinding in conventional equipment to pass a 6-mesh sieve. After crushing, the material is sent to the FluoDry unit for drying and dedusting. Fluidized Drying and Sizing As shown in Fig. 1, the FluoDry unit consists of a 1/4-in. cylindrical steel shell, 9-ft ID by 22-ft 6-in. overall height. Attached horizontally at the bottom is a 6-ft diam combustion chamber, approximately 7 ft 6 in. long. A refractory constriction dome, consisting of first-quality fire brick shapes, partitions the inside into two sections. The lower section is called the windbox and the upper the bed compartment. The vertical wall of the shell is lined with 6-in. first-quality rotary kiln blocks. In the bottom of the windbox a hoppered section is formed with castable refractory to permit the windbox to be readily cleaned via a 6-in. screw conveyor. The combustion chamber is similarly lined with refractory shapes. On the 6-in. diam section, 4 1/2 in. of insulating brick, HW-26, are used. The inner combustion chamber is lined with 4 1/2-in. Korundal brick to withstand the high flame temperatures encountered. An 8-in. steel feed pipe, entering vertically through the top and fitted with an air-operated cone valve,

Jan 1, 1952

By Robson Jacinto Coelho

A equipe da Coqueria identificou a possibilidade de reduzir o Burn Loss, que é a perda de material por queima durante o processo de coqueificação. Após uma série de estudos, utilizando a metodologia Seis Sigma, identificou-se oportunidades de melhorias operacionais que trariam mais eficiência, estabilidade operacional e consequente aumento na produção de coque e vapor, tais como: maior controle na admissão de ar, controle das perdas de coque e carvão, vedação dos fornos de coque e execução de paradas programadas específicas para Preservação Refratária, com foco na redução do back log e consequente prolongamento da vida útil das baterias de fornos de coque. A redução Burn Loss aumenta o rendimento coque/ carvão, com consequente redução do consumo específico de carvão e aumento na produção de coque e vapor. A implantação desse projeto permitiu a redução de 2,5 dólares por tonelada de aço produzida no Fiscal Year 16/17.

Oct 30, 2017

Develop a portable emissions measurement apparatus to sample and measure tailpipe concentrations of diesel particulate matter (DPM), carbon monoxide (CO), carbon dioxide (CO2), nitric oxide (NO), and nitrogen dioxide (NO2) under steady-state engine load and speed conditions during a 1-minute test.

Jan 1, 1994

Objective: To develop and test a training program that enhances the hazard recognition skills of underground limestone miners. This program can help job performance and lead to enhanced safety in the underground workplace.

May 1, 1998

By Rodrigo Afonso Hatwig

Os aços inoxidáveis duplex (DSS) e superduplex (SDSS) são ligas que se caracterizam por apresentar uma microestrutura composta por frações volumétricas similares das fases ferrita e austenita. Dependendo da composição química e do tratamento termomecânico aplicado, a microestrutura dos aços inoxidáveis DSS e SDSS poderá apresentar, além das fases ferrita e austenita, fases intermetálicas deletérias. Neste trabalho, um estudo termodinâmico-computacional foi realizado com o objetivo de acompanhar a evolução das fases de aços superduplex no intervalo de temperaturas entre 300°C e 1.200ºC. Para tanto, fez-se uso do software de simulação termodinâmica FactSage v. 6.4. Os resultados descrevem de forma eficaz as fases principais e secundárias em função da temperatura e composição química.

Aug 8, 2018

By A Trench, S Ulrich, S Hagemann

A synthesis of reported All-In Sustaining Costs (AISC) for 57 Australian gold mines in the period 2014–2016 reveals for the first time the clear influence of grade upon cost performance, most evident in gold-only underground mines. Past syntheses of costs on a single quarter basis have viewed grade as potentially subordinate to other factors such as production scale, mine geometry, mineralisation style and a combination of other mining-related costs. Better understanding of the grade to cost relationship on both an individual mine and whole-of-portfolio portfolio basis is needed. Insight into the roles and trade-offs between other cost-determining factors will aid the future sustainability of the gold mining sector in Australia and assist in targeting prospects for future resource growth and development. While the overall trend is toward higher-grade mines displaying lower costs and vice versa, the grade to cost functions appear radically different between mines based on time-series data. The median cost of Australian gold production in the final quarter of 2016 was A$1081/oz. The threshold for lowest cost quartile production was A$965/oz. Underground production now dominates Australian gold output – with 71 per cent of ounces originating from operations that are either entirely underground or hybrid pit/underground mines. Scale economies are evident, with smaller mines predominately among the higher cost producers. For mines of equal grade, open pit mines are lower cost than underground operations. Reserves are modest, with a median mine life for underground operations of 4.7 years based on current production rates. Reserve additions at mines are likely constrained not only by the finite nature of mineralisation at each mine but also by the geometrical difficulty of accessing suitable drilling locations to test for reserve extensions.CITATION:Ulrich, S, Trench, A and Hagemann, S, 2017. Towards an understanding of production costs at Australia’s underground gold mines, in Proceedings 13th AusIMM Underground Operators’ Conference 2017, pp 241–250 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Oct 16, 2017

By Sunil S. Gandhi

Magmatic-hydrothermal deposits rich in magnetite and/or hematite form a broad group that includes monometallic Fe deposits and polymetallic (mainly Cu and Au) deposits. They show a considerable variation in deposit characteristics, but share the genetic processes of magmatic differentiation and related hydrothermal activity in intermediate to felsic melts, and in some cases involve brines and/or meteoric waters during mineralization. They include several world-class deposits. They range in age from Proterozoic to Recent, and form important metallogenic districts in Scandinavian, Canadian, Brazilian and Australian Shields, Circum-Pacific regions, and in China, Iran and Turkey. Monometallic deposits have been important sources of iron in the past and still contain significant resources of the metal, e.g., the Kiirunavaara deposit in Sweden. The giant Olympic Dam Cu-Au-Ag-U-REE deposit was discovered in 1975, and since then explorationists have focussed on search for analogues worldwide. This has brought to light a number of economically important new deposits and prospects, including examples in Canada. The discoveries have in turn prompted considerable research on individual deposits and the group as a whole. This short paper is an attempt to summarize the main aspects of the group from the literature cited in Gandhi and Bell (1996), and from the papers published recently in two milestone volumes on these deposits, edited by Porter (2000 and 2002).

May 1, 2003

By Chandramohan P. V., Ravi Kishore

"An underground reservoir was to be constructed at Doha in Qatar. Simsima lime stone is present at the bottom. When the reservoir is empty, there will be uplift at the bottom but this will change to downward load when it is full. The rock at the bottom had high bearing capacity to resist downward load. But uplift had to be resisted by piles or anchors. The reservoir has a size of 120mx80m. Shrinkage and creep of concrete coupled with thermal contraction imposed a horizontal movement of 26mm on the extreme piles. So, piles have to accommodate this as well. This unique situation needed a unique solution. The solution was to provide piles with flexible high tensile strands to take tension. An annular space near the head of the pile would facilitate horizontal movement as well. Compression load was directly passed on to the raft bearing on rock.INTRODUCTIONAn underground reservoir for storage of drinking water was to be constructed at Doha, Qatar. The reservoir was proposed to have a plan size of 120m x 80m. Clear height inside the reservoir was proposed as 17.2m, from the bottom of roof to the top of bottom raft. Overall height of the reservoir at the outlet from the top of the roof to the bottom of raft was to be 21.2m. For the sake of inspection and in order to prevent pollution from the surroundings a gallery was planned around the reservoir. This could accommodate pipelines as well. This gallery was 3.0m wide on three sides and 8.4m wide on the outlet side.The gallery had removable gratings as cover in order to facilitate maintenance. Capacity of the reservoirwas proposed to be 40million gallons. The reservoir is divided into four compartments with baffle walls in each one for water circulation. Roof of the reservoir is kept at 300mm above ground level. There are two levels of car park on top of the reservoir. Top of the reservoir roof is at +14.35. Bottom varies from - 6.68 to -7.08. Lowest water table is at +6.00. Concrete structure of the reservoir was designed by a local consultant. The Navayuga Engineering Company was entrusted with the construction. Please see Figs 1 and 2."

Jan 1, 2017