Cleaning Mini Blast Furnace Gases with Gas Cleaning Plant

Industry:
Steel
Client:
Reputed Steel Manufacturing plant in Odisha
Year of Installation:
2013
About the Client –
  • Our client’s plant was incorporated in 1992 with assets in coastal Odisha in the eastern India. Its Pig iron plant is located at Jaipur which was successfully commissioned in 2005 and has since been operating uninterrupted.
Challenges

The process of liquid iron production in the Blast Furnace (BF) generates gas at the top of the furnace which is an important by-product of the BF process. The gas exiting at the top of the Blast Furnace is at a high temperature and pressure and usually contaminated with dust and water particles. This top gas has a substantial calorific value and is known as raw Blast Furnace gas, or contaminated Blast Furnace gas. The composition and quantity of this top gas depends on the nature of the technological process in the Blast Furnace, and the type and the quality of the raw materials used, for the iron production in the Blast Furnace. To further use the raw Blast Furnace gas, it is necessary to clean it by using certain process systems – which reduces its content of solid particles from 18 to 20 mg/Nm3, to less than 5 mg/Nm3 and reduces pressure as per the requirement of the downstream process.

The top gas contains Carbon Mono Oxide (CO) and is known as Blast Furnace gas after its cleaning. It is used as fuel gas for heating blast air in the hot blast stoves, as well as a supplemental fuel in the steel plant. For the BF gas to be used as a fuel gas, it is necessary that the raw Blast Furnace gas is cleaned and cooled, to reduce the volume of the gas along with the moisture content. Moreover, pressure also must be reduced. Furthermore, cooling and reduction in gas volume, is also necessary since it results in substantial savings in delivery costs throughout the extensive distribution system of the steel plant.

The Gas cleaning plant is designed for following varying input conditions and should deliver dust emission at the outlet as less than 5 mg/Nm3 and reduction in top pressure to 800-1000 mm WC.

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