Development and practice of the Falconbridge chlorine leach process

Canadian Institute of Mining, Metallurgy and Petroleum
E. O. Stensholt O. M. Dotterud E. E. Henriksen P. O. Ramsdal F. Stålesen E. Thune
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
4
File Size:
488 KB
Publication Date:
Jan 1, 2001

Abstract

"The development and commercial operation of the Falconbridge chlorine leach process have been described in papers in 1985 and 1987. Since this time, various process improvements have been implemented and the capacity of the Kristiansand refinery has been increased to 85 000 t/y Ni, 40 0000 t/y Cu and 4500 t/y Co. The focus has been on continuous improvements in productivity, the use of energy and other costs. Several environmental issues have also been eliminated or reduced since 1987. IntroductionThe first nickel refining operation in Kristiansand, Norway, started in 1910 based upon raw materials from Norwegian mines. In 1929, Falconbridge Nickel mines purchased the refinery to acquire information and the patent rights to the Hybinette refining process that was practised at the small Kristiansand refinery. Falconbridge ownership has now, for more than 70 years, provided a strong base regarding raw material supply, financial resources and technical support for further expansions and major technical improvements at the refinery.The main concepts of the new chlorine leach process were developed in the laboratories from 1966 to 1969 and the process was piloted from 1970 to 1972. The main stages in the commercial plant were started in the 1975 to 1981 period. After 1981, there have been a number of process modifications, plant expansions and improvements to operating practices. The developments up to 1988 have been described in previous publications (Stensholt et al., 1986, 1988).This paper presents an overview of the process and how it is practised at Falconbridge Nikkelverk AS (FNA) today and describes some of the main changes that have been implemented since 1988. During this time, the nickel capacity has been expanded from 54 000 t/y to 85 000 t/y and the cobalt capacity from 2000 t/y to 4500 t/y. The paper describes how these expansions were achieved together with continuous improvements in operating efficiency and also gives an overview of the main environmental concerns at the refinery."
Citation

APA: E. O. Stensholt O. M. Dotterud E. E. Henriksen P. O. Ramsdal F. Stålesen E. Thune  (2001)  Development and practice of the Falconbridge chlorine leach process

MLA: E. O. Stensholt O. M. Dotterud E. E. Henriksen P. O. Ramsdal F. Stålesen E. Thune Development and practice of the Falconbridge chlorine leach process. Canadian Institute of Mining, Metallurgy and Petroleum, 2001.

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