Tecnored Process-High Potential in Using Different Kinds of Solid Fuels

One important feature of the Brazilian Tecnored ironmaking process is its flexibility to use different types of solid fuels, other than metallurgical coke, as proved in the pilot plant tests by extensively using green petroleum coke, biomasses, high ash cokes, etc. Even if new solid fuels not thus far used are envisaged for a given project, thru the bench scale simulator of the process it is possible to predict the behavior of such solid fuels in the Tecnored furnace and establish the best techno-economical-environmental equation for its use. This paper discusses the key aspects involved in the use of alternative solid fuels in the Tecnored process.


Introduction
The unavoidable dependence on the use of metallurgical coke, has been appointed as the "Achilles' Heel" of the conventional blastfurnaces for the last years, earlier due to the constrains in the operation of environmentally harm coke ovens and more recently due to the worldwide shortage and skyrocketing prices of this raw material.
This new scenario of shortage and soared prices of coke has been created by the enormous steel demand on China, in turn the major exporter of coke.Despite the sharp increase in steel production in all continents, the coke exports from China have been kept at the level of 14 million tons, to attend internal demand, and therefore prices are much higher than the historical levels, as shown in Figure 1.
Since the massive installation of new coke-making capacities are unlikely to happen due to the tight environmental regulations and the high investment and construction time required, the development of new "coke-less" ironmaking technologies, seems to be crucial for the survival and growing of the steel industry in the coming years, specially for places short in metallurgical coal availability.
This paper discusses the flexibility of the Tecnored process as far as the use of alternative fuels to coke, is concerned.

Use of coke in blast-furnaces
Further in this work, the ability of the Tecnored process to dismiss the use of coke will be explained, but first is very important to understand why coke is so important in the conventional route.
Hot metal production via conventional blast furnace is closely linked with the use of coke and therefore its availability, according to the specifications, is of extreme importance.Coke plays three vital roles in blast furnace operation, namely: Physical, Thermal and Chemical 2 .
• Physical: Coke, especially as the only solid material downwards the melting zone, assures the necessary permeability to the furnace gas below, above and in the cohesive zone it self.Also, the coke bed works as a kind of basis to the huge weight of the overlying burden inside the reactor, requiring a suitable mechanical strength; • Thermal: The burning of the carbon content in the coke thru the oxygen of the hot blast provides most of the energy used in the process; and • Chemical: Coke is the carbon bearing material which gasifies and forms the reducing gas CO, needed for the indirect reduction of the iron oxides in the upper part of the blast furnace.Moreover, coke is responsible for the direct reduction of the remaining FeO, SiO, MnO, etc., and for the carburization of the molten iron.To reduce coke consumption in blast furnaces to the lowest possible level, there is a trend to increase the injection of pulverized coal, oil or other alternative reducing agents, although there is a technical limit for this practice.
On the other hand, to fully replace the use of coke, some steel producers have looked at the direct use of mineral coals in blast furnaces, but most likely the three roles cannot be attained and the hot metal production is unfeasible through this route.Typical problems in blast furnaces using mineral coals are the formation of accretions due to an unsuitable thermal profile inside the reactor, low heat value and high reactivity of mineral coals, low mechanical strength causing powder generation, etc.

Role of solid fuel in the tecnored process
Contrary to the conventional blast furnaces, the Tecnored technology has been conceived and developed to be a "coke-less" ironmaking process, thus avoiding the investment and operation of environmentally harm coke ovens besides significantly reducing green house gases emissions (GGE) in the production of hot metal, especially if compared to the blast furnace route.
The process uses two different inputs of carbon units: the reductant and the solid fuel, optimizing the flexibility of the process.The reducing agent, normally coal fines, but virtually fines of any type of carbon enriched material can be used, is added in the mixture which will form the self-reducing agglomerates (pellets or briquettes).The quantity of coal fines required is established by a C/F (Carbon to Iron Oxides) ratio, usually enough to achieve full reduction of the charge, by simple providing the needed heat for the process.In the self-reduction, the external CO does not play a significant role in the reduction process, as in the case of blast furnaces.
On the other hand, the lumpy solid fuel, also contrary to blast furnaces, is charged thru side feeders (to avoid the endothermic solution-loss reaction in the upper shaft) and is responsible to form the char bed and to provide most of the energy demanded by the process.This energy is formed by the primary blast (C + O 2 → CO 2 ) and by the secondary blast, where the upstream CO, generated by the gasification of the solid fuel at the hearth, is burned (CO + ½O 2 → CO 2 ). Figure 2 shows a schematic cross section of the Tecnored furnace, where these two important features are highlighted.
Depending of the ultimate function the two carbon units used in the Tecnored process, present distinct specifications, not only in terms of chemical composition, but also especially in size range.The solid fuel portion requires lumpy material, typically 40 to 80 mm, capable of handle the physical and thermal needs required form the solid fuels in the process, as shown in Figure 3.

Physical and thermal role
The lumpy coal used in the Tecnored furnace shall create the permeability in the hearth of the reactor for an even flow of the liquid and gaseous phase.Therefore, the solid fuel selected to be used in the process, in the ending-point of the side feeder, after the charification process, must to present a lumpy char, with an skeleton strong enough to support the load of the charge, besides a good reactivity to promote a suitable RAFT (raceway adiabatic flame temperature) and flame geometry, and finally able to create the desired CO / CO 2 ratio at the top of the char bed.
However, it is rather important to mention that the mechanical load imposed to the char bed is extremely small, due to the high volumetric productivity of the furnace, resulting on a much smaller reactor than a conventional blast furnace (Figure 4).This feature by itself is one of the main reasons that explains the ability of the furnace to dismiss the use of coke and allow the use of low-grade solid fuels.

Solid fuels tested
The list of solid fuels tested to be used in the Tecnored furnace is fairly extensive.Part of them has been effectively used and others have been approved after passing in the Process Simulator.

Solid fuels tested in the pilot-plant
The pilot plant development of the Tecnored process has been made in different phases, using different concepts and sizes of reactors (circular in the first phases and a modular slice of the industrial furnace in the last phase).During this period, a broad range of raw materials have been tested as charge and as fuel, always targeting the definition of the best furnace design, operation parameters, ultimate flame engineering, raceway pattern, melting zone formation and positioning, etc, in order to maximize the industrial furnace performance.All alternative solid fuels tested, previous to the hot operation with a ferrous burden, passed through a series of bench scale tests and process simulations in order to pre-approve its adequacy.These tests included but were not limited to, thermal shock, thermal degradation, cold test charging in the pilot furnace aiming at to evaluate the solid fuel angle of repose, distribution and segregation of different size fractions inside the reactor, etc.
The main types of solid fuels used in the pilot furnace, their typical composition and size range are shown in Table 1.
Figure 5 shows the fuel rate achieved in the hot metal production in the Tecnored pilot furnace for the different kinds of solid fuels and the specific ferrous burden used.
It is rather important to mention that the fuel rate indicated in Figure 5 is indicative only, since it varied in the trials as a function of the process parameters, ferrous burden type, Carbon/Oxide ratio in the self-reducing agglomerate, metallization degree of the DRI,  size range of the iron and carbon bearing materials, moisture, etc.Therefore, for each project based on a specific set of raw materials a different fuel rate shall be envisaged.
Additionally, one should remember that the consumption norms of the industrial furnace, compared to the pilot furnace, shall be considerably lower thanks to a better furnace engineering and control, higher top pressure, lower gas and heat losses through the walls, etc.
Therefore, the lump solid-fuels to the furnace can be selected from among a number of low-cost alternatives either to be used alone or mixed, as shown in Table 2 3 .
Each of the fuels listed above are very attractive but for some particularities the use of anthracitic coal, green petroleum coke and biomasses are of major interests.

Anthracitic coal
The mineral coal used in the Tecnored process is different from the ones feeding coke ovens for the production of metallurgical coke.

Green petroleum coke (pet-coke)
Pet-Coke is a by-product in the catalytic refining process of petroleum.Pet coke has virtually no gangue or ash.Downstream hot metal De-Sulfurization process and special gas cleaning systems can be applied in case of the use of high-sulfur crude.
The use of pet-coke is always a matter of cost equation.Presently, the cost of Petrobras, extensively used pet-cokes from Betim (Minas Gerais state) and Cubatão (São Paulo state), is two to three times cheaper than coke (≈ 80 US$/t of pet-coke against 250 US$/t of coke).
Brazilian pet-coke presents the following typical composition: • Fixed Carbon: 85%; • Volatile Matter: 12%; • Ashes: 1%; and • S: 0.7%.Pet-coke is found in three main types, depending on its physical structure: Needle, Shot and Sponge.Sponge coke is more porous and contains greater surface area, is usually desired from a marketer's viewpoint 5 and is the preferred pet-coke type to be used as fuel in the Tecnored process, although the three types can be used as reductant.From those three types, needle coke is the only intentionally produced from selected feedstock and therefore accounts for less than 5% of the current production in the world.

Biomasses
The use of renewable fuels in ironmaking is being pursued worldwide targeting a green based steel production, to assure a sustainable development of the sector.In this sense the use of biomasses seems to be the best possible clean route to economically produce primary iron, in a green house gases closed circuit where the CO 2 emissions are captured and recycled in the growing process of the biomass.
The following describes this cycle, as shown in Figure 6: • Carbon in the biomass is used as reductant and fuel in the ironmaking processes and becomes CO 2-e released to the atmosphere; • this CO 2-e is captured by the replanted biomass plantations, and used for plant growing through the photosynthesis; • the carbon is incorporated into the biomass and the oxygen is released to the atmosphere; and • aged biomass is used and the cycle starts over again.The carbon used in the process therefore is obtained by a nearterm closed cycle by the sequestration of the carbon from the atmosphere and not from the burning of fossil-fuel carbon.In addition, the low sulfur content in the biomass, results in very low SOx emissions 6 .
The Tecnored process can operate entirely with biomass, with the coarser fractions (charred or not) used as fuel and the finer fraction as reductant inside of the agglomerate.This carbon for reduction can be itself of biomass origin, such as charcoal fines or even other carbonized materials (grass, bagasse, coconut shells, corn-cobs, etc).The culture of fast growing biomasses (90 to 120 days) instead of eucalyptus (6 to 7 years) still opens the possibility for small farms participate in the iron production business, contributing for the social development of handicapped areas.
This can result in the complete use of the biomass to supply the entirely energy and reductant needs for pig iron production, assuring an environmentally friendly operation.In this approach the balance of GGE is negative, meaning that the overall sequestration of CO 2 from the atmosphere for biomass growing is higher than the CO 2 emissions during the production process.Furthermore, it opens the possibility to exploit the promising carbon credits marketing, estimated to range between 25.00 to 150.00 US$/ton of CO 2 traded, by 2015, depending on the location.
One good example to illustrate the use of biomass in the Tecnored furnace is the use of eucalyptus trees.In this case, the trunks and the thick branches portion of the tree can be used as fuel while the fine branches and leaves can be charred, ground, and used as reductant, implying in a more cost and environment effective use of the forest assets.

Figure 4 .
Figure 4. Elevation of a conventional blast furnace and a Tecnored furnace.

Table 1 .
Main types of solid fuels tested in pilot-plant.
* According to the norm ASTM/D-388, this is a sub-bituminous type of coal, although the trade company sells as an anthracite coal.** "Bracatinga" type wood, dried at open air yard.

Table 2 .
Solid fuels tested and approved for adequacy in the Tecnored furnace.