| Closed submerged arc furnace (SAF) | Electric arcs form beneath the burden, while carbonaceous reductants reduce chromium and iron oxides. The sealed furnace collects carbon monoxide-rich process gas. | Prepared chromite ore or agglomerates, reductant and flux; commonly used to produce high-carbon ferrochrome. | Enables controlled off-gas collection and can support energy recovery or use of furnace gas when suitable systems are installed. | Requires reliable feed preparation, gas handling, sealing and process control. Ore chemistry and burden permeability affect stable operation. | Large-scale production where consistent feed preparation and comprehensive gas-management systems are available. |
| Semi-closed submerged arc furnace | Uses submerged-arc smelting with a partially enclosed furnace roof and hood arrangement to capture much of the process gas. | Prepared chromite burden and reductant; commonly used for ferrochrome smelting. | Provides a balance between gas capture and access for furnace operation and maintenance. | Gas capture and workplace exposure performance depend on hood design, furnace practice and maintenance. | Operations seeking substantial fume collection with a configuration that allows routine access to the furnace top. |
| Open submerged arc furnace | Electric arcs operate below the burden, while the furnace top is not fully sealed; local extraction systems collect fumes around the furnace. | Prepared chromite burden, reductant and flux; used in ferrochrome production. | Offers direct access to the furnace top for charging and operating tasks. | Requires effective local fume extraction. Process gas is generally not captured as a sealed, concentrated stream. | Sites where open-top operation is established and suitable fume-control systems are in place. |
| DC arc furnace | Uses direct current and an electric arc, typically between an electrode and a conductive furnace hearth or bath, to supply heat for smelting. | May process chromite fines or other prepared chromium-bearing feed, depending on furnace design and operating practice. | Can offer flexibility for certain fine feeds and process configurations. | Application, feed requirements, electrode arrangements and operating economics are project-specific; it is not the default choice for every ferrochrome plant. | Projects where feed characteristics and technical studies support a DC smelting route. |
| Furnace selection: ore and burden preparation | Not a furnace type; this is a core design factor for choosing and operating a smelting furnace. | Chromite grade, particle size, gangue composition, moisture and the availability of lump ore, pellets or briquettes. | Matching the burden to furnace requirements can support stable electrical and chemical operation. | Fine or variable feed may require agglomeration or other preparation. Chromium recovery and slag composition depend on the full burden recipe. | All projects; representative ore testing and process design should precede equipment selection. |
| Furnace selection: energy and environmental systems | Compares power supply, electrode system, cooling, gas collection, dust removal and any off-gas energy-recovery equipment. | Applies to any furnace route and its site infrastructure. | Whole-plant evaluation can identify practical opportunities for energy efficiency and emissions control. | Performance depends on local electricity supply, plant layout, permitting requirements and the design of auxiliary systems. | All projects; compare total plant performance rather than furnace purchase specifications alone. |