Three-phase universal electromagnetic technological reactor for processing of minerals

Authors

  • V.G. Lukiaschenko Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • V.E. Messerle Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • A.B. Ustimenko Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • S.Kh. Aknazarov Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • Z.A. Mansurov Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • K.A. Umbetkaliev Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty
  • V.N. Shevchenko Institute of Combustion Problems, Bogenbai Batyr St. 172, 050012 Almaty; KazNU, al-Farabi st. 71, 050040 Almaty

DOI:

https://doi.org/10.18321/

Keywords:

reactor, mineral raw materials, electric smelting, melt

Abstract

This paper discusses the issues of technology and processing electromelting mineral rocks with a melting point up to 2200 K in a three-phase universal technological reactor. The results of thermodynamic calculations of melting various materials, including basalt, chrome waste sludge and dust cleaning chromium production are given. The calculations have shown that the gas and the condensed phases are no toxic substance, and in smelting slurry of monohromat toxic hexavalent chrome becomes completely secure trivalent. The results of experimental heats these minerals, which are defined on the basis of the optimal technological parameters of the reactor and shows promising processing minerals in their electromelting with electromagnetic stirring of the melt, are given. Thus, on the basis of calculated and experimental data, it is determined that the specific energy consumption for processing basalt and chromium sludge does not exceed 1 kW·h/kg, and the reduction of oxides of chromium carbides to it - 1.5 kW·h/kg.

References

(1) Ladue S. E. Progress Report on electric melting // The Glass Industry. — 1979. — June. — P. 12–16.

(1) Лукьянченко В. Г., Мессерле В. Е., Акназаров С. Х., Умбеткалиев К. А., Устименко А. Б., Шевченко В. Н., Сейсенова А. Б. Трехфазный универсальный электромагнитный технологический реактор (ЭМР) для переработки минеральных веществ // Сборник материалов VII Международного симпозиума «Горение и плазмохимия». — Алматы: Казак университеті, 2013. — С. 174–180.

(3) Лукьянченко В. Г., Мессерле В. Е., Устименко А. Б., Акназаров С. Х., Мансуров З. А., Умбеткалиев К. А., Сейсенова А. Б. Термодинамические расчеты переработки минерального сырья при его электроплавке в трехфазном электромагнитном реакторе (ЭМР) // Сборник материалов VII Международного симпозиума «Горение и плазмохимия». — Алматы: Казак университеті, 2013. — С. 216–221.

(4) Gorokhovski M., Karpenko E. I., Lockwood F. C., Messerle V. E., Trusov B. G., Ustimenko A. B. Plasma Technologies for Solid Fuels: Experiment and Theory // Journal of the Energy Institute. — 2005. — Vol. 78, No. 4. — P. 157–171.

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Published

2013-11-20

How to Cite

Lukiaschenko, V., Messerle, V., Ustimenko, A., Aknazarov, S., Mansurov, Z., & Umbetkaliev, K. (2013). Three-phase universal electromagnetic technological reactor for processing of minerals. Combustion and Plasma Chemistry, 11(4), 296-303. https://doi.org/10.18321/