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By T. Johnson

Hydrometallurgical processes can be exceptionally corrosive. This is particularly true in acid leaching processes for copper, cobalt, nickel and rare earth elements. In the last five years, several large hydromet plants have been built in North America (Vale - Long Harbour, Baja Mining ? El Boleo and MolyCorp - Mountain Pass). Hundreds of storage tanks, extraction vessels and electrowinning cells along with miles of piping were designed and fabricated to withstand the aggressive environments inherent in these processes. One key element all three projects had in common was the extensive use of FRP in equipment design. As a material of construction, FRP provided equal if not improved durability relative to alternative corrosion resistant alloys at a considerably lower cost. This paper will highlight the extensive use of FRP in these three world scale projects and why it was chosen for each process.

Jan 1, 2013

By D. G. Tisdale

A pilot plant was installed and operated at the Xstrata Nickel Sudbury Smelter 10 demonstrate the CANSOLV SO2 Scrubbing System. A 350 m3/h slipstream (through a 10cm pipe) was drawn from two different industrial gas streams to test the performance and robustness of the scrubbing system. The system achieved high sulphur capture, typically above 99%, and proved tolerant 10 varying gas strength and dust content in the feed gas.

Jan 1, 2009

By Mark Kennedy

New technology projects, particularly those involving first-of-a-kind metallurgical facilities, have a poor track record of achieving their overall financial targets, as they incorporate technological risks in addition to normal project risks. Traditional project management tools focus on risk from concept development through implementation, but typically fail to address the additional risks associated with a new technology project including slow start-up, slow ramp-up, and failure to achieve design performance (quality or throughput). These additional risks affect future cash flows produced by the project and hence its value, typically measured as net present value (NPV) or internal rate of return (IRR). Common accounting practice is to reduce the present value of future cash flows by applying a chosen discount rate, often reflecting the corporation?s cost of capital. This discount rate does not contain an allowance for technological risk, which is often underestimated or misunderstood by both the financial and engineering project managers. This paper will focus on the topic of project risk and new technology, and how these play a role in the probability of achieving the predicted future cash flows. By properly addressing technological risk in the form of risk-weighted returns, marginal projects can be prevented from proceeding, while sound projects can be given the additional time and resources required to achieve the optimal level of front-end-loading (the level which returns the maximum risk-weighted net present value). A simple set of mathematical tools should enable engineers and financial professionals to establish a common level of understanding, thereby leading to a more accurate assessment whether a new technology project is ready to pass through its next level of approvals.

Jan 1, 2013

By A. D. Dalvi

With the current economic situation, the demand for nickel and other base metals has fallen significantly. More than 440 kt/yr world nickel capacity has been taken out of production within the last year, or more than 25% of the total [1]. This situation is similar to that at the end of 1970?s and it will take a number of years for the demand to recover to the levels before the economic downturn. In the meantime, the challenges facing the industry have increased due to diminishing ore grades, more inaccessible and complex deposits, mounting capital and operating costs and the various external pressures which include socio-economic, environmental, and energy challenges. All industries will be faced with paying the ?total ownership costs? in the future. This will only increase the burden on the industry. How to cope with this in what Thomas Friedman calls the ?Energy-Climate Era? [2] will be the most pressing challenge for the next generation of metallurgists and managers. It will force us to take a broader view of the problems and the solutions beyond mere technical. The metallurgists, engineers and project managers will have to look at the overall projects and their objectives in designing the solutions, requiring a top-down strategic approach.

Jan 1, 2009

In view of the increasing environmental regulations that have been promulgated all over the world in the last 30 years, non-ferrous smelters and refineries have learnt and adapted to treat effectively metals'-containing process waste streams that need to be bled from the plant. However, anions such as sulfates, chlorides and fluorides-presently not a major problem ?are coming under increasing scrutiny and need to be addressed in the near future. The current paper reviews options for waste water treatment with reference to: a) types of waste streams processed b) process chemistry c) discharge options d) recovery and reuse of water and e) solids disposal. Methods to obtain zero liquid discharge ?a possible solution to eliminate discharge of above anions and residual heavy metals- are discussed with case studies. The long term goal of any non-ferrous smelter plant should be to have a zero liquid discharge philosophy-an approach that would become an epitome of water reuse and conservation.

Jan 1, 2009

By S. A. Shipilov

In this paper, the annual direct cost of corrosion in Canada is estimated to be approximately $41 billion. The figure does not include the indirect (user) costs of corrosion, sometimes referred to as social costs, which would essentially double the amount. Also, corrosion is shown to be a major contributor to environmental pollution, including when it results in the leakage of hazardous materials from pipelines, vessels and nuclear reactors. Industrial accidents caused by corrosion kill and injure hundreds of people annually. At present, corrosion is at the core of safety and risk analysis in several major industries such as energy generation, oil/gas production and transportation, chemical processing and petroleum refining. With the recent steam pipeline explosion during rush hour in New York killing one man, the collapse of the bridge in Minneapolis killing 13 people and another two years ago in Montreal when 5 people were killed, infrastructure corrosion is increasingly being acknowledged as a public safety concern.

Jan 1, 2009

By Chen Xia

Iron separation from rare earth elements has always been an essential operation in almost all steps of rare earth element recovery and purification processes. As RE3+ and Fe3+ behave similarly in many operations the separation can sometime be either difficult or cost-inefficient. This article attempts to review the methods and options for removing the iron content within the process, with the focus on the existing or proposed precipitation and solvent extraction technologies. The precipitation of iron from REE solution as iron hydroxide, jarosite, goethite, hematite, or phosphate are briefly introduced. Methods for precipitating REE from solutions leaving iron impurities in the aqueous phase are discussed. Some proposed solvent extraction flow sheets for separating iron from REE are conceptually reviewed in this article.

Jan 1, 2013

The NorthMet deposit of PolyMet Mining contains a large reserve of copper-nickel-cobaltprecious metal mineralization. Historically it has been difficult to recover separate copper and nickel concentrates of a quality broadly acceptable to custom smelters using conventional mineral processing techniques. Recently, improved flotation methods have made it possible to produce separate and saleable concentrates which will be produced during initial startup of the NorthMet deposit and construction of the PLATSOL TM hydrometallurgical plant. After the initial transition period, it is planned that production of a bulk flotation concentrate will be followed by PLATSOL TM hydrometallurgical treatment to produce copper, nickel/cobalt and precious metal products. The PLATSOL TM process uses chloride-assisted total pressure oxidation treatment of a bulk concentrate to digest the base and precious metal content of the bulk concentrate into an autoclave solution. Following solid-liquid separation, the solution is then treated sequentially for precious metal recovery by reductive precipitation, copper solvent extraction and electro winning and finally, nickel and cobalt recovery by precipitation. During the pilot plant testing of the PLA TSOUM process for NorthMct bulk concentrate treatment, two variations on nickel and cobalt recovery were tested including mixed hydroxide precipitation with magnesia and separate nickel and cobalt hydroxide precipitation following solvent extraction separation with Cyanex 272. The results of the pilot plant testing of the nickel and cobalt recovery circuits for NorthMet arc presented.

Jan 1, 2009