pp43-45 MS06 - Millennium Steel
Transcription
pp43-45 MS06 - Millennium Steel
2.2 MS06-25 pp43-45 2/6/06 5:03 pm Page 43 RAW MATERIALS AND IRONMAKING HYL direct reduction With the acquisition by Techint Technologies of HYL Technologies, Techint is now the second largest international producer of DRI with 12 modules producing more than 7Mt of DRI a year. The HYL process produces DRI with 94% metallisation with up to 4.5% carbon and can be directly linked to the EAF for hot charging. he strategic acquisition by Techint Technologies of HYL Technologies has many affinities with the existing activities of the company and extends the range of technologies and services offered for the steelmaking industry. The HYL process produces direct reduced iron (DRI) which is used mainly to produce steel in electric furnaces, together with or as an alternative to steel scrap. T HISTORY Although the use of smelted iron objects can be traced back as far as about 2000BC, the direct reduction of iron on a commercial industrial scale has only been a successful enterprise since the HYL process was first introduced in the mid-1950s by the Mexican steelmaker Hojalata y Lamina (later Hylsa) who developed a batch process for using natural gas to reduce iron ore for use in EAF steelmaking. In reality it is more appropriately a petrochemical rather than a steelmaking technology, since the process involves using the reducing agents from a gas source (natural gas, syngas, coke oven gas, etc) to chemically remove the oxygen from iron ore, thus producing a purified iron (DRI) for melting in a steelmaking furnace. Lack of availability of steel scrap made this invention a necessity for Hylsa and in subsequent years the technology continued to be modified and improved. It was, however, a technology for Hylsa’s own use and the first licences granted to outside companies for using the technology were not so much ‘sold’, as ‘purchased’. Although plants in Mexico, Brazil, Venezuela, Iran, Iraq and Indonesia using the original HYL technology were later licensed, the focus continued to be primarily on Hylsa’s own requirements rather than on the external market. In the mid-1970s the department in charge of direct reduction became the technology division of Hylsa. The HYL Technology Division, now HYL Technologies, immediately focused on updating its technology to a continuous shaft furnace process that it had developed earlier, and to commercialise the process worldwide. The growth of the electric furnace steel industry has substantially increased the demand for DRI, a product that is particularly suitable for the production of highquality steel, and HYL Technologies is now one of the world leaders in the design and supply of direct reduction plants, with valid patented technologies that have been widely tested. Although the company’s history has for the most part been dedicated to providing technology solutions for in-plant applications, HYL has consistently been the innovator in providing new and improved technologies and solutions which then became the standard for others to follow (see Table 1). Two significant examples are HYL ZR®, a highly efficient direct reduction process which works without the traditional gas reformer, and the HYTEMP® system, a solution for continually feeding electric furnaces with a Date Event 1957 Start-up of the first commercially successful gas-based direct reduction plant. 1957 Production of flat products via the EAF, based on the use of DRI. 1958 Batch charging of DRI to the EAF at 600°C. 1965 Use of more than 30% DRI in an EAF charge practice. 1968 Continuous feeding of DRI to the EAF. 1968 Computerised EAF process control system put into use. 1969 Use of foamy slag practices. 1970 Design of pellets for direct reduction. 1970 Production of extra-deep drawing steels in EAF using DRI. 1972 Use of 100% DRI in an EAF charge practice. 1980 Start up of the HYL process continuous shaft furnace in Monterrey. 1986 Implementation of CO2 removal and capture as salable by-product. 1988 Use of cement coating of pellet/lump ores for direct reduction. 1993 HYTEMP pneumatic transportation system and hot DRI feeding to the EAF. 1994 Production of high carbon DRI (3.0–4.5%). 1997 World’s first dual-discharge (DRI & HBI) plant design put into operation, Vikram Ispat-Grasim, India. 1998 Startup of first HYL ZR Process plant, Hylsa 4M, Monterrey. 2000 High Carbide Iron™, unique product of the ZR Process. 2003 Development of HYL Micro-Module for requirements of small steel plants. r Table 1 Industry firsts from HYL MILLENNIUM STEEL 2006 AUTHOR: Carlos Garza HYL Technologies, SA de CV 43 2.2 MS06-25 pp43-45 2/6/06 5:06 pm Page 44 r Fig.1 HYL ZR, Process schematic hot DRI, thus increasing the productivity of the steelworks and reducing power consumption. MILLENNIUM STEEL 2006 HYL ZR PROCESS 44 The HYL ZR process is a major step in reducing the size and improving the efficiency of direct reduction plants. Reducing gases are generated by in-situ reforming in the reduction reactor, feeding natural gas as make-up to the reducing gas circuit and injecting oxygen at the reactor inlet (see Figure 1). Since all reducing gases are generated in the reduction section, optimum reduction efficiency is attained, and thus an external reducing gas reformer is not required. In addition to lower operating and maintenance costs and higher DRI quality, the total investment for a ZR plant is typically 10–15% lower when compared to a DR plant which includes a reformer. The overall energy efficiency of the ZR process is optimised by the integration of partial combustion, prereforming and in-situ reforming inside the reactor, as well as by a reduced requirement for thermal equipment in the plant. A significant advantage of this process is the wide flexibility for DRI carburisation, which enables controlled carbon levels in the DRI up to 5.5% to be attained. This is possible due to the improved carburising potential of the gases inside the reactor which allow for the production of iron carbide. For the production of high quality DRI (94% metallisation, 4% carbon and hot discharged at 700°C), the energy consumption is 2.25–2.40Gcal/t DRI of natural gas and 60–80kWh/t DRI of electricity. The iron ore consumption of 1.35–1.40t/t DRI is very low, mainly due to the high operating pressure of the process. The impact of eliminating the external gas reformer on plant size is significant. For example, a plant of 1Mt/y capacity requires only 60% of the area needed by other process plants for the same capacity. For additional capacity, the area required is also proportionally smaller in comparison since, for example, the same reactor size would be used for a 1 million or a 1.5 million t/y facility, and only the other related equipment would increase in size. This also facilitates locating the DR plant adjacent to the melt shop in existing operations. This plant configuration has been successfully operated since 1998 with the HYL DR 4M plant and in the 3M5 plant in 2001, both at the Ternium Hylsa facility in Monterrey. It was the reformer-less ZR process that allowed HYL to develop a 200kt/y capacity Micro-Module, reversing the tendency to ever-increasing module sizes and providing quality DRI capability for small steel mills. HYL plants can also use conventional steam-natural gas reforming equipment, which has long characterised the process, together with other reducing agents such as hydrogen, gases from coal, petroleum coke and cokeoven gas depending on the particular situation and availability. HYTEMP SYSTEM The HYTEMP system is a pneumatic system for the transport of hot DRI to the EAF (see Figure 2), using nitrogen or process gas as the transport gas. It is an environmentally friendly process since the DRI is kept enclosed from the time of discharge from the reduction reactor to the discharge into the EAF. The system has the flexibility for feeding two EAFs from the same reduction reactor. At the bottom of the reactor, DRI is discharged to the HYTEMP system where a hot gas flow coming from the gas heater is circulated and used to transport DRI. To avoid degradation the DRI is transported by pressure build-up rather than velocity of the gas. When hot DRI reaches the storage bins on top of the EAF the DRI and gases are separated. The gas is sent to a scrubber to be cleaned and cooled, compressed and gas heated for recycling. Before entering the gas heater, make-up gas is added to compensate for losses when separating DRI from the transport gas. Hot DRI separated from the transport gas is sent to a transition bin in order to go from the pressure of the transport system to atmospheric pressure. From the transition bin DRI goes into the storage bin to be fed into the EAF by gravity. Hot DRI can also be sent from the reduction reactor to an external cooler when the melt shop is not ready to use or store hot DRI. The external cooler has the capacity to cool all DRI production. FUTURE PROSPECTS Techint is now the second-largest international producer of DRI with 12 modules installed in Siderca, Sidor, Matesi and Hylsa and currently produces over 7Mt of 2.2 MS06-25 pp43-45 2/6/06 5:09 pm Page 45 RAW MATERIALS AND IRONMAKING r Fig.2 HYL HYTEMP system HYL Technologies has already acquired a contract for the turnkey installation of a 200kt/a Micro-Module plant in Abu Dhabi based on the ZR process. Additional projects already announced are for the upgrading of the Mittal Steel Lazaro Cardenas HYL plant in Mexico, which will reduce that plant’s natural gas consumption by 20%; as well as a new ZR Process DR module for Vikram Ispat-Grasim in India, also adding 500kt/y of capacity to their existing installation. Other projects are in advanced stages of negotiation and are expected to commence later this year. MS Carlos Garza is Director General, HYL Technologies, SA de CV, Monterrey, Mexico. CONTACT: carlos.garza@hyltechnologies.com MILLENNIUM STEEL 2006 direct reduced iron a year. It is also the fourth largest producer of electric steel in the world and was one of the first users of DRI. This is further confirmation of the strategic importance of HYL Technologies for Techint. The worldwide network of Techint Technologies will be of great help in promoting HYL Technologies worldwide. The product of HYL Technologies traditionally involves supplying a technological package generally comprising process engineering, detailed engineering of certain sections, main components, assembly assistance, including staff training, and the licence to use the technology. Tying in with other Techint technologies such as electric furnaces, materials handling and quality systems for melt shops will make attractive packages for clients looking for the most advanced solutions for their operations. 45