Synergic effects of activation routes of ground granulated blast-furnace slag (GGBS) used in the precast industry

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Synergic effects of activation routes of ground granulated blast-furnace slag () used in the precast industry Martin Cyr, Cédric Patapy To cite this version: Martin Cyr, Cédric Patapy. Synergic effects of activation routes of ground granulated blastfurnace slag () used in the precast industry. 26. HAL Id: hal-344929 https://hal.archives-ouvertes.fr/hal-344929 Submitted on 2 Jul 26 HAL is a multi-disciplinary open access archive for the deposit and dissemination of scientific research documents, whether they are published or not. The documents may come from teaching and research institutions in France or abroad, or from public or private research centers. L archive ouverte pluridisciplinaire HAL, est destinée au dépôt et à la diffusion de documents scientifiques de niveau recherche, publiés ou non, émanant des établissements d enseignement et de recherche français ou étrangers, des laboratoires publics ou privés. Public Domain

Synergic effects of activation routes of ground granulated blastfurnace slag () used in the precast industry Martin CYR, Cédric PATAPY 2,2 LMDC, Université de Toulouse, INSA, UPS, France Martin.Cyr@insa-toulouse.fr, 2 Cedric.Patapy@insa-toulouse.fr Abstract - Ground granulated blast-furnace slag () is a common by-product used for decades in the cement and concrete industry, and having beneficial effects on environmental properties and durability of concretes. However, reacts less rapidly than cement and the short-term compressive strength of -concretes are usually lower than the ones of Portland cement concretes. The aim of this paper is to test the efficiency and evaluate the synergic effect of combining different activation routes (fineness of Portland cement and, use of chemical activation, and application of thermal cycles) on shortterm compressive strength of -Portland cementbased materials. Results showed that the simultaneous use of all activation routes allowed blended cement with to achieve almost the same initial mechanical characteristics than Portland cement. Keywords - ground granulated blast-furnace slag, activation, temperature, fineness I. INTRODUCTION Ground granulated blast-furnace slag () is a common supplementary cementing material (SCM) used for decades in the cement and concrete industry. is a by-product of the steel industry, rapidly quenched with water and ground to a fineness similar to that of a Portland cement. The main components of are CaO (3-%), SiO 2 (28-38%), Al 2 O 3 (8-24%), and MgO (-8%). has been recognized to have beneficial effects on environmental properties (lower CO 2 production than Portland cement) and durability of concretes. Examples of durability improvement of -based concretes are numerous and can be found easily in the literature [-3]. However, reacts less rapidly than cement and the shortterm compressive strength of -concretes are usually lower than the ones of Portland cement concretes. This situation could be a problem in domain such as the precast industry, where the short-term strength (e.g. between 6h and 24h) must be high enough to maintain the rate of production of concrete elements. On the one hand, solutions exist to improve the short-term strength of concrete. They are based on mainly three approaches, most of the time used separately: increase the fineness of the, increase the temperature of curing by applying thermal cycles to the concrete, or use chemical activators to enhance the reactivity of the. On the other hand, it is well known that the increase of the cement fineness generally improves its reactivity, especially at short term. The combination of all of these methods is not often found in the literature, but it could represent a real opportunity to counteract the limited reactivity of at young ages by exploiting the synergy between the different activation routes available. The use of higher amount of could thus improve the long term durability of the concretes, without the inconvenient of the lack of performance at very short term. The precast industry is well adapted to the combination of all these activation routes, especially because of the possibility to increase the temperature of concrete curing. The aim of this paper is to test the efficiency and evaluate the synergic effect of combining different activation routes (fineness of Portland cement and, use of chemical activation, and application of thermal cycles) on short-term compressive strength of -Portland cement-based materials. II. MATERIALS and METHODS The Portland cement was a CEM I 2. N CE CP2 NF as specified in European Standard NF EN 97- [4]. Its chemical composition is given in Table I and its original fineness was 4 cm 2 /g (Blaine specific surface). A highly amorphous industrial (chemical analysis in Table I) was used at two finenesses: 43 and 68 cm 2 /g. The aggregate used in mortar production was a normalized quartz sand conformed to NF EN 96- with particle size ranging between and 2 mm []. The sodium sulfate used for the activation of the systems was from analytical grade. The experimental program was carried out on mortars prepared according to NF EN 96- []. The mass of binder (cement or cement+) was kept constant at 4 g. Granular-to-sand ratio and water-to-binder ratio were set at 3 and., respectively. A reference mortar composed of % of Portland cement was prepared and cured at 4 C and 6 C for 6h. Sixteen mortars with were cast to evaluate the effect of the following parameters (illustrated in Fig. ):

- content: % and 7% - fineness: 43 cm 2 /g and 68 cm 2 /g, two industrial grades available - cement fineness: 4 cm 2 /g and 78 cm 2 /g, the last one being obtained after a grinding of min in a laboratory grinder. Formulation - temperature of curing: 4 C and 6 C in climate chambers - chemical activation:.8% Na 2 SO 4 Cement fineness fineness Temperature of curing Chemical activation % % cement 4 cm 2 /g 43 cm 2 /g 4 C 7% 3% cement 8 cm 2 /g 68 cm 2 /g 6 C Fig. Schematic representation of the 6 mortar mixtures containing.8% Na 2 SO 4 The samples were cast in 4x4x6 cm polystyrene molds, sealed in plastic bags and allowed to harden at two different temperatures: 4 C for 6h or 6 C for 6h (compressive strength test ), followed by a cure at 2 C until the age of test (compressive strength test 2). The compressive strength results were the mean of three values. TABLE I PROPERTIES OF CEM I AND Components CEM I CaO 67.4 4.3 SiO 2 22.84 36.8 Al 2 O 3 2.7.44 Fe 2 O 3.84. SO 3 2.23.93 Na 2 O.4.34 K 2 O.23.44 Loss on ignition (LOI).72 - Specific gravity, g/cm 3 3.3 2.9 Mass-median-diameter (D), m 2.6 2.8 Blaine Surface area (m 2 /g) 4 43 III. COMPRESSIVE STRENGTH RESULTS Fig. 2 presents the compressive strength results at 6h and 24h of all mortar mixtures. For the same mixtures, Fig. 3 gives the strength activity index, defined as the ratio of compressive strength of mortar and reference mortar. Four activations routes were investigated: cement fineness, fineness, chemical activation (only at one level) and increase in the curing temperature. It can be seen that some activation routes were better than others to improve the strength of -Portland cement mixtures. Individual activation route cannot alone allow the mixture to challenge the Portland cement. The only combination which led to the better results was the increase in the temperature to 6 C, with fineness of cement and at their maximum levels. Several observations can be made: - When the curing temperature was set at 4 during 6h (followed by a cure at 2 C), no combination of activation routes allowed us to reach, neither at 6h nor 24h, the reference mortar composed of commercial CEM I. The better result at this curing temperature (SAI of.74) was obtained after 24h for the mortar mixture with the finest cement and (8 and 68 cm 2 /g, respectively). - The curing temperature of 6 C during 6h led to much better results, as it was possible to reach or get close to the reference at 6h and 24h for % mortars made with the finest cement and (8 and 68 cm 2 /g, respectively). When 7% of was used, the strength at 6h approached 9% of the reference with the same combination of cement- fineness. However, the strength activity index decreased at 24h (.72), probably due to a blockage effect sometimes seen when the hydration is strongly activated [6]. - When the cement fineness was kept at 4 cm 2 /g, and by combining fine (68 cm 2 /g) and high temperature (e.g. 6 C), it was possible to almost reach the reference cured at 4 C (for %- mixtures at 6 and 24h, and 7%- mixture at 6h). It means that it could be possible to avoid the cement grinding by combining high fineness and temperature of curing higher than the reference CEM I. Fig. 4 presents the increase in strength (in %) when a given parameter went from a minimum value to a maximum value. All the calculations were made by taking mortars 2 by 2 with only one parameter changing, all the others remaining equals. For example, when the fineness went from 43 cm 2 /g to 68 cm 2 /g, several increases were calculated with constant values of cement content (3 or %), cement fineness (4 or 8 cm 2 /g), and curing temperature (4 or 6 C). Fig. 4 gives the mean increase of the values, as well as the minimum and maximum increases obtained. 2

Compressive strength (MPa) Compressive strength (MPa) Compressive strength (MPa) Compressive strength (MPa) It can be seen (inside the min and max values of each parameter chosen in this study) that all parameters did not have the same effect on the increase in strength at young ages: - The curing temperature had a huge effect on the strength at 6h, as passing from 4 C to 6 C led to a significant increase in strength between 9 and 3%, with a mean value of +74%. - This effect was much less important at 24h, the gain being at a mean value of +38% - The effect of fineness was in the same order of magnitude at 6h and 24h, with mean increase values between +36 and +39% when the fineness of the went from 43 to 68 cm 2 /g. - The cement content fallowed a similar trend, meaning that % (i.e. % of cement) led logically to the better results. - The increase of the cement fineness was the less significant parameter, as the mean increase in strength were at average values of +3-7%, although a significant effort to increase the fineness (4 to 8 cm 2 /g). However, it should be kept in mind that the increase in cement fineness could help reaching the goal of approaching the reference mortar when it is combined to other activation routes ( fineness and temperature). 4 % 7% 4 3 3 6h 3 2 2 CEM I at 4 cm 2 /g. 9. 9..6 9.9 26.8 6.9 22.3 8.6 27.4 3 2 2 4..6 4.6.8 9.9 26.8.9 9.. 23.7 4 C 6 C 4 C 6 C 24h 4 3 3 2 2 8.9 2.4 2. 2.3 37.2 34. 2.9 3. 2. 3.6 4 3 3 2 2.8 6. 2.9 2.9 37.2 34. 6.8 23.8 2. 26.8 4 C 6 C 4 C 6 C Fig. 2 Compressive strength at 6h and 24h of mortars cured 6h at 4 C or 6 C. Reference mortars contained % CEM I (4 cm 2 /g), while mixtures ( and 7% of fineness: 43 or 68 cm 2 /g) were made with cement of fineness 4 or 8 cm 2 /g. 3

Increase in strength (%) % 7% 6h.9.8.7.6..4.3.2..4..46.8.63.83.69.2.9.8.7.6..4.3.2..2.28.23.29.44.7.6.89 4 C 6 C 4 C 6 C 24h.9.8.7.6..4.3.2...63.9.74.9.82.67.96.9.8.7.6..4.3.2..3.47.38.6.4.64.7.72 4 C 6 C 4 C 6 C Fig. 3 (defined as the ratio of compressive strength of mortar and reference mortar) at 6h and 24h of mortars cured 6h at 4 C or 6 C. Max 74% Mean increase Min 64% 3% 39% 36% 38% 3% 7% 6h 24h 6h 24h 6h 24h 6h 24h Cement content 3 % Cement fineness 4 8 fineness 43 68 6h temperature curing 4 6 C Fig. 4 Increase in strength (in %) when a given parameter went from a minimum value to a maximum value (example: fineness from 43 cm 2 /g to 68 cm 2 /g) 4

IV. ENERGY CONSUMPTION An analysis based on a simple calculation of the energy demand when is used as cement replacement is presented. The calculation is based on the energy consumed for the production of cement and, which includes the manufacturing (e.g. heating of cement raw meal) and the final grinding of the material (clinker, ). It excludes the energy for thermal treatment at 4 and 6 C since the comparisons are made here for mixtures cured at the same temperature. The energy required (E, in kwh/t of binder) is given by equation, as a function of the binder composition, and of the energy needed for the manufacturing and the grinding of cement and. A calculation of the performance energy E performance (in kwh/t/mpa) can also be proposed (equation 2), by dividing the required energy E by the compressive strength of the mortar containing the binder under consideration. E performance gives the energy cost of each MPa of strength. grinding grinding E + E + E E E{in kwh/t} = C cement cement () - E Eperformanc e {in kwh/t MPa } = (2) Strength where E is the energy consumption (in kwh) for the production of one ton of binder, C and are the proportions of cement and in the binder respectively, grinding E and cement E are the energy consumption (in cement kwh/t) of the cement manufacturing and the finish grinding of the material, respectively, grinding E and E are the energy consumption (in kwh/t) for the and the grinding of the material, respectively, E is the energy consumption for the performanc e production of one ton of binder, relative to the compressive strength of the mortar containing the binder considered, Strength is the compressive strength of the mortar of composition C+ The data used for the calculations were taken from the literature and are reported in Table II [7-2]. The total energy required to produce cement was evaluated to be in the range 8-2 kwh per ton of cement, including around kwh/t for the finish grinding of the clinker. In the case of, the energy was assumed to be kwh/t (as it is a byproduct). The energy for grinding is recognized to be higher than for clinker, due to the presence of hard glass. According to various authors [,2], % more energy is necessary to reach the same fineness for as for clinker. Manufacturing Finish grinding TABLE II DATA USED FOR THE CALCULATION OF ENERGY CONSUMPTION Energy consumption (kwh/t) Cement Ref Ref E = 9 a cement [7-9] From the steel plant grinding E = or 2 cement [9,] Grinding E = --- a values in the literature between 8-2 kwh/t for dry (initial data in GJ/t, with 3.6 GJ = kwh) grinding E = 7 or 2 [,2] The results of the calculations are given in Figs. and 6 for all the composition studied. (a) Energy requirement of binder E, in kwh/t of binder Fig. When ton of binder was considered, the energy consumption with was always lower than for the reference with only cement (Fig. ). This means that ton of binder with had a lower energy cost (almost proportional to the cement remaining in the system), although the grinding of required more energy than the grinding of clinker. remained less energy consuming because of the absence of energy demand of the manufacturing. (b) Performance energy E performance, in kwh/t/mpa Fig. 6 When the energy consumption was considered relative to the performance of mortars (for instance compressive strength at 24h for mortars cured at 6 C), it can be seen that: - The use of systematically (for these conditions) involved a decrease in the energy consumption per MPa, meaning a better energetic efficiency of the system. - The best E performance were obtained for fine, whatever the fineness of the cement. - It is possible to obtain good E performance with up to 7% of. This means that, from a "performance energy" point of view, it is better to use fine without considering the fineness

C4 C4-S43 C4-S68 C8-S43 C8-S68 C4-S43 C4-S68 C8-S43 C8-S68 Energy consumption (grinding) per MPa (kwh t - /MPa) C4 C4-S43 C4-S68 C8-S43 C8-S68 C4-S43 C4-S68 C8-S43 C8-S68 Energy consumption per ton of binder (kwh t - ) of the cement. These mixtures lead to the best efficiency of the, i.e. more performance (in terms of MPa) for a given energy: each MPa cost less kwh per ton of binder. 9 8 7 6 4 3 2 % C % 7% Fig. Energy consumption of mortars containing. Energy requirement of binder (E, in kwh/t of binder). 3 2 2 26.9 24. 8. 23. 6.9 2. 6.3 7.8.3 % C % 7% Fig. 6 Energy consumption of mortars containing. Performance energy (E performance, in kwh/t/mpa) for mortars cured at 6 C (for 6h), then tests for compressive strength at 24h. V. CONCLUSION This paper aimed at evaluating the possibility of using blended cements in the precast industry as a challenger to Portland cement used alone. Combinations of four activation routes were tested on % and 7% mixtures. The following conclusions can be drawn: - In heated systems (such as in precast industry), it is possible to challenge, in terms of compressive strength, Portland cement at 6h and 24h, when combining chemical activation, the fineness of the, the fineness of the cement and a curing temperature of 6 C. - The best activation route is the temperature, followed by the fineness of the. - The cost of each MPa (per kwh per ton of binder) is lower with fine used in replacement of the cement. A possible perspective to optimize the mixtures would be to add fine limestone filler (LF) to improve the packing, as and LF are known to work well together. VI. REFERENCES [] M. Öner, K. Erdoğdu and A. Günlü, Effect of components fineness on strength of blast furnace slag cement, Cem Concr Res, Vol.33, pp. 463 469, 23. [2] D. M. Roy, Alkali-activated cements opportunities and challenges, Cem Concr Res, Vol.29, pp. 249 24, 999. [3] M. C. G. Juenger, F. Winnefeld, J. L. Provis and J. H. Ideker, Advances in alternative cementitious binders, Cem Concr Res, Vol.4, pp. 232 243, 2. [4] EN 97- Cement - Part : Composition, specifications and conformity criteria for common cements, 22. [] EN 96- Methods of testing cement - Part : Determination of strength, 26. [6] E. Marciano and A. F. Battagin. The Influence of Alkali Activator on the Early Hydration and Performance of Portland Blast Furnace Slag Cement, in ICCC Gothenburg, Sweden. 997. [7] I.Z. Bribián, A.V. Capilla, A.A. Usón, Life cycle assessment of building materials: Comparative analysis of energy and environmental impacts and evaluation of the eco-efficiency improvement potential, Build Environ, Vol.46, pp.33-4, 2. [8] J.A. Moya, N. Pardo and A. Mercier The potential for improvements in energy efficiency and CO 2 emissions in the EU27 cement industry and the relationship with the capital budgeting decision criteria, J Clean Prod Vol.9, pp.27-2,2. [9] C. Hosten and B. Fidan, An industrial comparative study of cement clinker grinding systems regarding the specific energy consumption and cement properties, Powder Technol, Vol.22, pp.83-88, 22. [] D. Touil, S. Belaadi and C. Frances, Energy efficiency of cement finish grinding in a dry batch ball mill, Cem Concr Res, Vol.36, pp.46-42, 26. [] R.H. Snow, T. Allen, B.J. Ennis and J.D. Litster, Size reduction and Size Enlargement. Perry RH, Green DW (ed). Perry's Chemical Engineers' Handbook. 7 th Edition. McGraw-Hill; 997. [2] J.N. de la Vergne, The Hard Rock Miner s Handbook. 3 rd Edition. McIntosh Engineering: North Bay; 23. 6