Calcined Petroleum Coke

Calcined Petroleum Coke

Calcined petroleum coke is a critical ingredient in the production of aluminum. It is created by placing high quality raw "green" petroleum coke into rotary kilns, where it is heated to temperatures between 1200 to 1350 ˚C (2192 to 2460 ˚F). The high temperatures remove excess moisture, extract all remaining hydrocarbons and modify the crystalline structure of the coke, resulting in a denser more electrically conductive product. In a matter of hours, calcined petroleum coke is cooled from 1350 ˚C to less than 200 ˚C, when it can be safely handled and transported to storage silos or placed directly into shipping containers, trucks, railcars, barges or vessels.

Calcined petroleum coke has a sponge-like structure which plays an important role in the making of anodes. The pores allow binding material to penetrate through the coke particles and form a solid carbon block, through which aluminum smelters conduct electricity into their smelting pots. Over time, the anodes are consumed, roughly at the rate of 40 tons of calcined petroleum coke for each 100 tons of aluminum produced. Currently, there is no known commercially viable substitute for calcined petroleum coke in the fabrication and utilization of aluminum smelter anodes.

Feature of calcined petroleum coke

Petroleum coke after calcination:

  • Eliminate volatile matter and moisture in raw materials. After calcination, the volatile matter of calcined petroleum coke is less than 0.5%, and the moisture content is less than 0.3%.
  • The volatile content and moisture of the calcined coke represent the degree of calcining. If it fails to meet the requirements, it will shrink twice and form cracks during calcining.
  • The density and mechanical strength of calcined petroleum coke is improved. The true density is above 2.00g/cm3. The true density of the calcined coke affects the true density of the final product. The poor mechanical strength and the low bulk density affect the molding mainly due to difficulty in molding. The height of the green agglomerate cannot meet the requirements within the required time and affects the operation of the aluminum electrolytic cell. The main manifestation is slag drop.
  • The conductivity of Calcined petroleum coke improved. The specific resistance of calcined coke affects the resistivity of the final product.
  • The chemical stability of Calcined petroleum coke improved. The oxidation resistance of calcined petroleum coke improved.
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