Patent Application
20180171422
The present invention relates to a method for solidifying liquid steel slag to produce solid steel slag, in particular solid steel slag which can be used, after crushing, as aggregate in construction. This method comprises the steps of pouring at least four successive layers of said liquid steel slag, comprising a lowermost layer, an uppermost layer and at least two intermediate layers, and cooling the solidified steel slag in the reservoir by applying water thereon. The liquid steel slag comprises at least the elements calcium, silicon and oxygen and has a basicity, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as SiO2, which is higher than 1.2 so that when it is slowly cooled down, at a cooling rate of for example about 10° C./min, β-dicalcium silicate is formed therein as from a first temperature.
Steel slag is a calcium silicate slag which contains in particular dicalcium silicates but also other silicates such as for example calcium magnesium silicates. A problem of such calcium silicate slags is that, upon slow cooling thereof, for example in the open air, a lot of them disintegrate into a fine powder. This is due to the formation of crystalline dicalcium silicate (C2S) phases which undergo several phase transformations during the cooling of the slag. The last transformation, which is the transformation from the β to the γ-polymorph, occurs at about 490° C., and is accompanied by a 12% volume expansion. This expansion causes high internal stresses in the slag and as a result thereof the disintegration of the solid slag into a fine powder. In contrast to the larger solid steel slag pieces, which can be crushed to produce an aggregate that can be used in construction materials such as concrete and asphalt, the fines cannot be used as such in these applications, i.e. due to their high water absorption properties, and are thus difficult to valorise.
As described for example in the article “Options to prevent dicalcium silicate-driven disintegration of stainless steel slags” of Y. Pontikes et al. in Archives of Metallurgy and Materials, Volume 55, Issue 4, several potential routes are already known for avoiding the formation of γ-dicalcium silicate. These potential routes include the chemical stabilization of the slag by additions such as borates and phosphates, the change in slag chemistry by the addition of waste glass and a fast cooling (quenching or granulation) of the liquid slag.
By the addition of borates and phosphates the transition of the β to the γ-polymorph of dicalcium silicate can be prevented or the amount of γ-polymorph which is still formed can at least be reduced. A drawback of borates is however their relatively high cost. Moreover, borates have been found to be toxic so that at least in a number of countries they are or will be forbidden. In Europe, for example, due to the validity of REACH (EC Regulation No. 1907/2006 concerning the Registration, Evaluation, Authorization and Restriction of Chemicals), the addition of borates creates a major problem with regard to the stainless steel slag stabilization. The borates are considered to be toxic for the reproduction and are part of the CMR (Carcinogenic, Mutagenic or Toxic for the Reproduction) list of substances. Phosphates have to be used in larger amounts than borates and involve therefore also a relatively high additional cost.
By adding waste glass, or any other material that contains a large amount of silica such as quartz sand or fly ash, the chemistry of the steel slag can be changed, i.e. the basicity thereof can be reduced, so that the presence of C2S can be avoided. To avoid the formation of C2S, the slag composition should conform to either one of the following relations:
CaO+0.8MgO≤1.20SiO2+0.39Al2O3(+1.75S) CaO≤0.93SiO2+0.55Al2O3(+1.75S)
To meet either one of these relations, a quite large amount of waste glass has to be added. Sakamoto (in “Effects of MgO based glass addition on the dusting of stainless steel slag” in Current Advance in Material and Processes, 14(4):939, 2001) showed for example on a laboratory scale that stainless steel decarburization slag could be stabilized with 12 wt. % of waste glass containing 70-75 wt. % SiO2. Although the cost of such glass addition is much lower than the cost of a borate addition, an additional slag treatment process is required to be able to dissolve such large amount of glass in the industrially used slag pots. Additional heat required to dissolve the glass could for example be generated by injecting oxygen in the slag pot. If the slag contains FeO, the injected oxygen could react exothermally with this iron oxide to produce Fe2O3. This additional treatment involves additional time and costs and requires the presence of a sufficient amount of FeO in the slag. The required amount of glass cannot be added to the steel furnace itself since low basicity slags cause rapid refractory degradation and, in stainless steel making, low chromium yields. The present inventors have done tests wherein a relatively large amount of waste glass was first applied in a slag pot before the liquid steel slag was poured therein. Although the heat of the liquid slag was high enough to melt the glass, a problem was how to mix the glass homogeneously in the liquid slag and this without too many heat losses. For large amounts of glass, only a part of the waste glass melted. A drawback of an incomplete melting of the glass is that glass inclusion can be formed in the solid slag which, when used as construction material, may cause deleterious swelling reaction as a result of the so-called alkali-silicate reactions.
The third route of reducing or avoiding the formation of γ-dicalcium silicate consists in a fast cooling of the steel slag. As set forth in the above-mentioned article of Y. Pontikes et al. the cooling rate required to avoid the formation of γ-dicalcium silicate is however quite high. This cooling rate should be about 5° C./s. A drawback of such a fast cooling process is that the required cooling rate cannot be achieved in a slag yard where the slag pots are poured out and the steel slag is solidified by air-cooling, even when this air-cooling is assisted by spraying water onto the solidified slag. A very fast cooling can only be achieved by an air or water granulation technique wherein the liquid slag is solidified and cooled down in a jet of air or water. Due to this fast cooling, a large portion of the solidified steel slag is moreover amorphous (glassy), which is not desired when using the steel slag as an aggregate in concrete or in road constructions. Indeed, the amorphous phases bind less strongly to cement and also reduce the polished stone value (PSV) of the aggregate (determined for example in accordance with BS EN 1097 Part 8), which is an important parameter when used in road constructions. Indeed, in the construction of a road, the surface layer needs to retain its roughness for as long as possible in order to provide skid resistance for traffic. The higher the polished stone value the longer the aggregate will remain rough when used in road surfacing. A final drawback of water or air granulation techniques are that a quite fine aggregate is produced, which is less valuable than coarser aggregates.
Tests wherein a steel slag is solidified by means of a water granulation technique are disclosed for example in the article “Treatments of AOD slag to Enhance Recycling and Resource Conservation” by Q. Yang in Proceedings of Securing the Future, Int. Conf. on Mining and the Environment, Metals and Energy Recovery, Jun. 27-Jul. 1, 2005, Skelleftea, Sweden. Slow cooling, at an average rate of about 60° C./min from 1550° C. to 623° C., resulted in a low glass content (3%) but a lot of fines (90% smaller than 100 μm) whilst fast cooling by water granulation, within less than one minute, resulted in a high glass content of about 24% and a particle size between about 0.2 and about 3 mm.
Water granulation tests, wherein the liquid steel slag is solidified within one minute, are also described in the article “Dissolution Behavior of Fluorine in AOD slag from the Production of Stainless Steel after Treatment for Volume Stabilization” by Q. Yang et al. A. 2012 Scanmet IV: 4th International Conference on Process Development in Iron and Steelmaking. Luleå: MEFOS, Vol. 2, p. 517-526. By water granulation the presence of γ-dicalcium silicate could be avoided whereas by more slowly cooling the slag, within about 5 hours from 1600° C. to room temperature (i.e. at an average cooling rate of about 5° C./min), γ-dicalcium silicate was still formed.
Tests wherein a steel slag is solidified by means of an air granulation technique are disclosed for example in the article “Stabilization Studies of EAF Slag for Its Use as Materials in Construction” by Q. Yang et al. in Proceedings, Asiasteel 24 Sep. 2012, The Chinese Society for Metals, 6 p. In the air granulation test, wherein the steel slag was cooled down in an air stream in about one minute, the slag was stabilized so that no fines were produced. In the slow cooling test, wherein the slag was again cooled down within 5 hours from 1600° C., i.e. at an average cooling rate of about 5° C./min, the slag disintegrated into fines.
An object of the present invention is to provide a new method for solidifying a liquid steel slag which enables to reduce the formation of fines, or in other words the formation of γ-dicalcium silicate, by a cooling process which does not require a fast cooling, i.e. a cooling rate of at least 5° C./s, and which in particular does not require an air or water granulation step so that the formation of relatively large amounts of amorphous/glassy phases can be avoided.
To this end, the method according to the present invention is characterised in that
In the method of the present invention the steel slag is cooled by means of water which is applied on top of the uppermost layer. Due to the large volume of the layers of solidified steel slag, and the relatively low thermal conductivity thereof, the fast cooling rate of at least 5° C./s required to prevent the transition of β to γ-dicalcium silicates cannot be achieved by applying water on top of the solidified layers of steel slag. As a matter of fact, it takes several hours, or even days, to cool down a large volume of steel slag. According to the invention it has however now been found that, even without a fast cooling of the liquid steel slag, in particular without an air or water granulation of the liquid steel slag, the formation of γ-dicalcium silicate can still be considerably reduced by keeping the steel slag for a sufficiently long period of time at a relatively high temperature, in particular at a temperature which is higher than the temperature at which β-dicalcium silicate is formed.
The method of the present invention thus comprises two cooling phases, namely a first cooling phase wherein the liquid steel slag is allowed to solidify and kept for a period of time at a relatively high temperature of between 1300° C. and the temperature as from which β-dicalcium silicate is being formed, and a subsequent second cooling phase wherein the solidified steel slag is further cooled down with water, in particular at least until the temperature of each of the intermediate solidified slag layers is lower than 400° C., preferably lower than 300° C. and more preferably lower than 200° C. During this second cooling phase, the intermediate slag layers are cooled down relatively fast to a temperature which is lower than the temperature at which the transition from the β to the γ-polymorph of dicalcium silicate takes place (which occurs in pure dicalcium silicate at a temperature of about 490° C.).
The first cooling phase is intended to allow the formation of crystalline phases different from dicalcium silicate phases. These crystalline phase comprise in particular calcium magnesium silicate (CMS) phases such as merwinite (C3MS2), bredigite (C7MS4) and diopside (CMS2). They are formed by crystallisation of the liquid phases contained in the steel slag and also by transformation of the dicalcium silicate phases which are formed at higher temperatures, in particular from α and/or α′-dicalcium silicate phases. It was found that during the subsequent second cooling step, considerably less dicalcium silicates are formed which may be explained by the fact that β-dicalcium silicate is formed less easily/quickly from calcium magnesium silicate phases than from α or α′-dicalcium silicate phases.
In a preferred embodiment of the method according to the invention, the minimum temperature above which the temperature of each of the intermediate layers is kept at least until the start of the water cooling step is equal to or higher than 700° C., preferably equal to or higher than 750° C., more preferably equal to or higher than 800° C., most preferably equal to or higher than 850° C. and even more preferably equal to or higher than 900° C.
These temperatures are all higher than the temperature at which β-dicalcium silicate is formed. In pure dicalcium silicate the transition from α′ to β-dicalcium silicate occurs indeed at 675° C. A higher temperature is however preferred in particular when bredigite is formed in the steel slag. Bredigite (C7MS4) is indeed a metastable phase which is only stable at higher temperatures. At lower temperatures, it may transform again into dicalcium silicate phases. By keeping the temperature higher, more bredigite, if formed, thus remains in the slag.
In another preferred embodiment of the method according to the invention the temperature as from which β-dicalcium silicate is formed in the steel slag when cooling the liquid steel slag down to room temperature is lowered by adding a phosphorus containing compound to the liquid slag, in particular a phosphate and/or a pyrophosphate containing compound.
It has been found that by adding a phosphorus containing compound to the liquid steel slag not only the transition from β to γ-dicalcium silicate is reduced but also the temperature as from which β-dicalcium silicate is formed is lowered. In the method according to the present invention, the temperature of the different layers can thus be kept more easily sufficiently high to avoid the formation of β-dicalcium silicate during the first cooling phase.
In a further preferred embodiment of the method according to the invention, the basicity of the liquid steel slag, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as wt. % SiO2, is lowered by adding a glassy material thereto after the liquid steel slag has been separated off from the liquid steel, which glassy material has a further basicity, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as wt. % SiO2, which is smaller than 0.20, and preferably smaller than 0.15. The glassy material comprises preferably at least 50 wt. %, more preferably at least 60 wt. % silicon expressed as SiO2. The glassy material preferably comprises glass that has preferably been crushed, in particular soda-lime-silica glass.
A first effect of the addition of the glassy material is that the basicity of the steel slag is lowered so that less dicalcium silicate is formed therein upon cooling. The glassy material is however preferably applied in relatively small amounts, which can be dissolved more easily homogenously in the liquid slag but which are not enough to avoid entirely the formation of dicalcium silicates.
Another effect of the addition of the glassy material is that upon cooling of the liquid slag less bredigite is formed therein and more merwinite. In contrast to bredigite, merwinite has the advantage of being a stable phase. Consequently, even when the temperature of the steel slag during the first cooling phase is somewhat lower, merwinite remains as such in the steel slag and can thus not increase the formation of dicalcium silicate phases below a certain temperature at which bredigite would no longer be stable.
Other particularities and advantages of the invention will become apparent from the following description of some particular embodiments of the method according to the present invention. The reference numerals used in this description relate to the annexed drawings wherein:
The present invention relates to a method for solidifying liquid steel slag to produce solid steel slag. The solid steel slag is a calcium silicate slag which may contain different crystalline phase such as dicalcium silicate phases, calcium magnesium silicate phases and other phases. The steel slag is in particular a stainless steel slag. It can in particular be an AOD (Argon Oxygen Decarburization), a VOD (Vacuum Oxygen Decarburization) an EAF (Electric Arc Furnace) slag or a combination thereof. When the steel slag consists of steel slag materials of different origins, they do not have to be mixed but they can be applied separately on top of one another as described further hereinafter.
In order to be able to valorise the resulting solid steel slag as much as possible, it should contain a minimum amount of fines, in particular a minimum amount of particles smaller than 0.5 mm. These fines are mainly the result of a disintegration of the slag which is driven by the irreversible β to γ-C2S phase transformation causing a volume expansion of about 12%. During this phase transformation high internal stresses thus occur in the slag, as a result of which the slag disintegrates into fine particles. The coarser part of the solid steel slag can be used, after crushing and sieving, as fine or coarse aggregates, in particular in concrete and asphalt. Dicalcium silicate phases are formed in the steel slag when the steel slag has a basicity, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as SiO2, which is higher than 1.2 so that the present invention is intended to solidify such steel slag material whilst reducing or preventing the formation of fines, having in particular a size of less than 0.5 mm.
In accordance with the present invention the amount of fines is reduced by a particular cooling method. In practice the liquid slag which is separated off from liquid steel, in particular from liquid stainless steel, is applied in a slag pot 1 and is transported in this slag pot 1 to a slag yard. When the liquid slag is applied in the slag pot, it has a temperature which is usually higher than 1500° C., for example in the range of 1550° C. to 1750° C. Before being transported to the slag yard, and during the transport itself, the liquid slag cools down in the slag pot, depending on the residence time in the slag pot.
As illustrated in
Each of the successive layers is usually applied by pouring one slag pot 1 in the reservoir. However, it is also possible to pour two or more slag pots 1 at the same time, or shortly after one another (so that the steel slag from the first slag pot has not solidified yet, for example with a time interval of less than 5 minutes), in the reservoir so that the liquid slag of these slag pots 1 flows together and forms one layer of liquid steel slag 2 in the reservoir 3. After having poured the uppermost layer 7 in the reservoir 3, water is applied, in particular sprayed, onto the steel slag in the reservoir 3 to cool the solidified steel slag layers 6-8. This water cooling step is preferably started at least one hour, preferably at least two hours and more preferably at least three hours after having poured the uppermost layer 7 of liquid steel slag 2 in the reservoir 3. In this way, the intermediate layers 8, which are intended to produce a solid steel slag with less fines, are kept for a longer time at a higher temperature before cooling them down with water. The water cooling step is preferably started less than ten hours, preferably less than seven hours and more preferably less than five hours after having poured the uppermost layer 7 of liquid steel slag in the reservoir 3. In this way, the intermediate layers 8 are not allowed to cool down to a too low temperature before they are cooled more quickly with water.
An important feature of the present invention is indeed that the temperature of each of the intermediate layers 8 should be kept at least until the start of the water cooling step, i.e. until the moment water is applied onto the uppermost layer, and this for at least one hour and preferably for at least two hours, between 1300° C. and a minimum temperature which is equal to or higher than the temperature as from which β-dicalcium silicate is formed in the steel slag when the liquid steel slag is cooled down to room temperature, in particular at a cooling rate of about 10° C./min. This temperature can be determined by means of a DTA analysis (Differential Thermal Analysis) wherein the steel slag is cooled down for example at a rate of about 10° C./min. The temperature of each of the intermediate layers 8 is defined herein as a volume weighted average over the respective intermediate layer. If ⅓th of the layer has a temperature of 700° C., ⅓th a temperature of 720° C. and ⅓th a temperature of 750° C. then the temperature of the layer is equal to ⅓×700° C.+⅓×720° C.+⅓×750° C.=723° C.
The minimum temperature is preferably equal to or higher than 700° C., more preferably equal to or higher than 750° C., most preferably equal to or higher than 800° C., and even more preferably equal to or higher than 850° C. or even equal to or higher than 900° C. The temperature of each of said intermediate layers 8 (determined as a volume weighted average over the respective intermediate layer 8), is preferably kept before the start of said water cooling step, for at least one hour, preferably for at least two hours, below 1200° C., and preferably below 1100° C.
During this first slow cooling phase, at these relatively high temperatures, crystalline phases different from dicalcium silicates are formed. The steel slag usually comprises not only the elements calcium, silicon and oxygen but also magnesium (in an amount which is preferably higher than 4 wt. %, more preferably higher than 6 wt. % and most preferably higher than 8 wt. %). The presence of magnesium causes the formation of calcium magnesium silicates, in particular of merwinite and/or bredigite, during the first cooling phase at these relatively high temperatures rather than dicalcium silicates, more particularly rather than α′-dicalcium silicates. Dicalcium silicates (α or α′) which were formed at higher temperatures are being transformed during this first cooling phase into other crystalline phases, in particular into calcium magnesium silicate phases. During the subsequent cooling phase with water, these crystalline phases, which are different from dicalcium silicate, transform less easily into β and subsequently into γ-dicalcium silicate so that by increasing the amount of these crystalline phases the disintegration of the steel slag can be considerably reduced.
The successive layers 6-8 of liquid steel slag 2 are poured at predetermined temperatures and at predetermined time intervals on top of one another in said reservoir 3. The temperature of each of these intermediate layers 8 can be kept above the above described minimum temperature by keeping said predetermined temperatures sufficiently high and said predetermined time intervals sufficiently short. The predetermined time intervals are in particular shorter than 90 minutes, preferably shorter than 75 minutes, more preferably shorter than 60 minutes and most preferably shorter than 50 minutes. The predetermined temperatures of the liquid steel slag 2 upon being poured in said successive layers are in particular higher than 800° C., preferably higher than 900° C. and more preferably higher than 950° C. or even higher than 1000° C. In order to enable the different layers of liquid steel slag to solidify to some extent before the next layer is poured on top thereof, the predetermined intervals between the different pouring steps are preferably longer than 5 minutes, more preferably longer than 10 minutes and most preferably longer than 15 minutes.
The intermediate layers 8 should further have a sufficiently large average thickness to avoid a too quick cooling of the steel slag in the respective layer (before a next layer is applied on top thereof) and to enable to produce a sufficiently coarse aggregate by crushing the solidified steel slag within each intermediate layer 8. When the bottom 4 of the reservoir 3 has a surface area of S m2, the intermediate layers 8 should each have a volume of at least S×0.03 m3 so that the intermediate layers 8 have an average thickness of at least 0.03 m. The volume of the intermediate layers 8 is preferably at least S×0.04 m3 and more preferably at least S×0.05 m3.
The intermediate layers 8 are preferably not too thick so that the steel slag is of a more uniform temperature within each layer. In this way too hot areas, wherein in particular α-dicalcium silicate could be formed instead of calcium magnesium silicates during the first cooling phase, and/or too cold areas wherein in particular β-dicalcium silicate could already be formed, can be prevented. The volume of the intermediate layers of liquid steel slag is therefore preferably at most S×0.5 m3, more preferably at most S×0.4 m3, most preferably at most S×0.3 m3 and even more preferably at most S×0.2 m3.
The temperature of each of the intermediate layers 8, determined as a volume weighted average over the respective intermediate layer, drops preferably at an average rate which is not higher than 50° C./min, preferably not higher than 40° C./min, more preferably not higher than 30° C./min and most preferably not higher than 20° C./min as from having applied the liquid steel slag until the layer is being covered by a further intermediate layer 8 or by said uppermost layer 7. This slow cooling rate can be achieved by allowing the intermediate layer to cool by air cooling, i.e. by being in contact with the atmosphere. Avoiding higher cooling rates is advantageous in view of the fact that by these relatively low cooling rates, the produced solid steel slag contains a smaller amount of amorphous phases (compared to the existing processes wherein the steel slag poured in the slag yard is immediately cooled down by water spraying to achieve a fast cooling limiting the transition of β into γ-dicalcium silicates). Preferably the cooling rate is so low that the produced solid steel slag contains less than 10 wt. %, preferably less than 7 wt. %, and more preferably less than 5 wt. % of amorphous phases. An advantage of such small amounts of amorphous phases is that the aggregates produced from the steel slag have a high PSV value. Although less preferably, a small amount of water could be sprayed on top of the different successive layers 6-8 to accelerate the cooling/solidification of the steel slag before a next layer is applied on top thereof but this amount should not be too large to prevent a too fast cooling of the steel slag and to enable to maintain the temperature of the intermediate layers above the above described minimum temperature until the actual cooling step with water. In this respect, the reservoir is preferably shielded off from the rain.
During the water cooling step, water is applied onto the uppermost steel slag layer 7. This water is applied preferably at least until the temperature of each of said intermediate layers 7 (i.e. their volume weighted average temperature) is lower than 400° C., preferably lower than 300° C. and more preferably lower than 200° C. Applying water onto the uppermost steel slag layer 7 is preferably stopped when the temperature of this uppermost steel slag layer 7 is still higher than 100° C. In this way all of the applied water evaporates resulting in a dry steel slag material. The cooling water is preferably sprayed onto the uppermost steel slag layer 7 and is applied preferably at such a flow rate that no water accumulates onto the uppermost steel slag layer 7, i.e. so that the flow rate at which the water is applied is equal to or smaller than the rate at which the water evaporates. It was found that in this way the most effective cooling of the steel slag layers 6-8 could be achieved.
The successive steel slag layers 6-8 have preferably a total height of less than 2.0 m, preferably less than 1.8 m, more preferably less than 1.6 m and most preferably less than 1.4 m. In this way, a sufficiently quick cooling of all of these layers can be achieved by applying water on top of the uppermost layer 7.
The liquid steel slag 2 has a predetermined basicity, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as wt. % SiO2. This basicity is in particular so high that upon a slow cooling of the steel slag, dicalcium silicates are formed leading to a (partial) disintegration of the steel slag, i.e. to a so-called dusting or falling of the steel slag. The basicity is more particularly usually higher than 1.2, in particular higher than 1.4 and often higher than 1.6. The basicity of EAF slags is usually lower than the basicity of AOD or VOD slags. EAF slags may have for example a basicity of about 1.4 whilst AOD slags have for example a basicity of 1.7 or even higher so that AOD slags are more prone to dusting than EAF slags.
In the method of the present invention, the basicity of the liquid steel slag is preferably lowered by adding a glassy material thereto after the liquid steel slag has been separated off from the liquid steel. This glassy material has a basicity, defined as the ratio between its calcium content, expressed as wt. % CaO, and its silicon content, expressed as wt. % SiO2, which is smaller than 0.20, and preferably smaller than 0.15. The glassy material preferably comprises at least 50 wt. %, more preferably at least 60 wt. % silicon expressed as SiO2 and comprising in particular glass, preferably waste glass, that has preferably been crushed. The glass may in particular be soda-lime-silica glass. Such glass is available as waste material and is known as glass cullet. The glassy material preferably comprises magnesium, in particular in an amount of at least 1.0, preferably at least 2.0 wt. %. An advantage of additional magnesium is that it can contribute in the formation of calcium magnesium silicate phases. Moreover, in case of the steel slag comprises chromium, for example stainless steel slag, a magnesiochromite spinel phase can be formed which reduces the leaching of chromium from the steel slag.
The glassy material can be admixed to the liquid slag when the liquid slag is being poured in the slag pot 1. It is however easier to apply the glassy material separately into the slag pot, in particular by applying it in the slag pot before introducing (pouring) the liquid steel slag therein. Tests have demonstrated that when introducing 3 wt. % of glass cullet in the slag pot before pouring the liquid steel slag therein (having a temperature higher than 1500° C.), more than 99% of the glass cullet dissolved in the liquid steel slag. More glass cullet could be dissolved in the liquid steel slag by injecting the glass cullet in the steel slag which is being poured in the slag pot. When injecting for example about 5 wt. % of glass cullet in the flow of liquid steel all of the glass cullet dissolved therein. Calculations have shown that when adding for example 15 wt. % of glass cullet (having a temperature of 25° C.) to the liquid steel slag, the temperature thereof only drops with somewhat more than 200° C. so that the liquid steel slag contains enough heat to dissolve quite large amounts of glass cullet.
The glassy material is however added to the liquid steel slag in an amount which is preferably less than 10 parts by weight, preferably less than 9 parts by weight and more preferably less than 8 parts by weight, per 100 parts by weight of the liquid steel slag. The smaller the amount of glassy material, the easier it can be dissolved homogeneously in the liquid steel slag.
An advantage of the addition of a glassy material to the liquid steel slag is that the basicity of the liquid steel slag is reduced. More importantly, however, in combination with the above described solidification method of the present invention, the addition of a glassy material has additional, synergetic effects. Indeed, the addition of glass reduces the formation of bredigite during the first cooling phase and increases the formation of merwinite. This effect can already be demonstrated at relatively low amounts of glassy material. The reduction of the amount of bredigite in favour of the formation of other calcium magnesium silicate phases has the important advantage that, in contrast to these other phases, bredigite is metastable and may thus lead to the formation of dicalcium silicate upon cooling of the steel slag, in particular during the water cooling phase. Due to the large volume of solidified steel slag contained in the different layers, a fast cooling thereof (as by water or air quenching) is indeed not possible.
The above described effects of the solidification method of the present invention and also of the special effects of the addition of glass in combination with this solidification method can be explained based on the following calculations. These calculations are made for an average AOD slag having the following composition:
Calculations were made on the equilibrium mineralogy to be expected at different temperatures with the FactSage Slag-A model with manual addition of bredigite (Ca7MgSi4O16 or C7MS4), with a stability range of about 900-1300° C. On the C2S behaviour, the model could only predict the transition to γ from α′ directly. β-C2S was not considered a stable phase as it only forms because it is easier to nucleate than γ-C2S. In practice, a transition from α′-C2S to β-C2S occurs, and further a transformation from β-C2S to γ-C2S (destructive and to be avoided) occurs if not blocked by boron (and/or quenching).
The following phases were indicated in
In
A further calculation was made with the same model but with the addition of glass. The glass had the following composition:
As potassium is not modelled well in the FactSage databases, the K2O content was added to the Na2O content.
Upon addition of glass at 25° C. to the slag at 1600° C., the temperature of the slag dropped drastically as shown in
The following phases were indicated in
When comparing
To further reduce the formation of fines, the usual borates can be added to the liquid slag. These borates reduce the transition of β to γ-dicalcium silicate. An additional advantage of the addition of borates is that they lower the temperature of the phase transformation from α′ to β-C2S. In pure dicalcium silicate α′-C2S transforms to β-C2S at a temperature of 675° C. A differential thermal analysis (DTA) has been carried out on dicalcium silicate doped with 0.13 wt. % of disodium tetraborate (Na2B4O7). The α′ to β phase transition occurred at an average temperature of 638° C., i.e. at a temperature which is about 37° C. lower than the temperature at which this phase transition occurs without the addition of borate.
A same effect can be achieved by the addition of a phosphorus containing compound. A DTA analysis has also been carried out on dicalcium silicate doped with 2 wt. % of a composition composed of about 50% CaF2 and about 50% of {(Ca5(PO4)3OH)+(Ca5(PO4)3F)}. The α′ to β phase transition occurred at an average temperature of 641° C., i.e. at a temperature which is about 34° C. lower than the temperature at which this phase transition occurs without the addition of the phosphorus containing compound. In contrast to borates, such phosphorus containing compounds, in particular phosphate and/or pyrophosphate containing compounds, have no toxic effect and can thus freely be added to the liquid steel slag. The phosphorus containing compound does not only reduces the transformation from β to γ-C2S but also lowers the temperature as from which γ-C2S is formed when cooling down the liquid steel slag. In this way, it is thus easier in the method of the present invention to keep the layers of steel slag during the first cooling phase at a temperature which is higher than the temperature at which γ-C2S starts to be formed in the steel slag.
In this experiment slag pots wherein liquid AOD slag was allowed to cool to a temperature lower than 1000° C. were poured in layers in a reservoir without a fast cooling with water. This resulted in an amount of fines of more than 80%. When pouring the slag pots in layers in the reservoir when the steel slag still had a temperature of at least 1000° C., and when subsequently cooling the stack of layers by spraying water onto them, a solidified steel slag which contained nearly no fines was obtained.
A same experiment was done, with the same AOD slag, with a combination of hot (>1000° C.) and cold (<1000° C.) slag pots. In one test the amount of hot pots was 55% and the amount of cold pots 45%. This resulted in 20% of fines. A combination of 2% of hot pots and 98% of cold pots resulted in about 80% of fines.
22 slag pots with varying amounts of liquid steel slag (AOD and EAF) were poured at different temperatures (mainly due to different residence times in the slag pots) and at different time intervals in a slag reservoir having a bottom with a surface area of 6×20 m2. The total height of the stack of layers was about 1.4 m. 4.5 hours after having poured the uppermost layer in the reservoir, water was sprayed on top of it. The surface temperature of each of the layers was measured just before pouring the next layer on top of it and the temperature was also measured in the lowermost layer and in the first intermediate layer, i.e. in the layer applied on top of the lowermost layer. The average temperature of each of the layers just before a next layer was applied thereon was calculated by means of a temperature model. The dicalcium silicate (C2S) contents and the calcium magnesium silicate (CMS) contents (sum of merwinite, bredigite and diopside) of the different layer was measured after the solidification and cooling of the layers. The different results are indicated in the following table.
In this experiment an amount of borates was added to the AOD steel slag to avoid the transition from β to γ-C2S. Due to the low basicity of the EAF slag, i.e. a basicity of about 1.4, no borate was added thereto. The AOD slag had a basicity of about 1.8.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/EP2014/056341 | Mar 2014 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2015/056777 | 3/27/2015 | WO | 00 |
