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IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 148
INVESTIGATION ON THE ACTIVATING EFFECT OF NA2CO3 AND
NAOH ON SLAG
B. Yuan1
, Q.L. Yu2
, H.J.H Brouwers3
1
Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands
2
Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands
3
Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands
Abstract
This study aims to investigate the activating effect of Na2CO3 and NaOH on the workability and mechanic strength of slag-based
alkali activated materials with different alkali contents and water to binder ratios. The heat release during the reaction process of
slag activated with sodium carbonate and sodium hydroxide were monitored respectively to analyze the hydration process.
Meanwhile, the workability and compressive strength were also tested with two types of activators (Na2CO3 and NaOH), two
different dosages (5% and 7% of equivalent Na2O by slag weight) and three different water to binder (W/B) ratios (0.37, 0.45 and
0.5). The results show that the reaction process of slag activated with sodium carbonate is much slower than that of sodium
hydroxide activated one, and its reaction phase happens approximately 40 h after the dissolution phase, and in all cases, sodium
carbonate gives the higher fluidity and compressive strength with the same Na2O content and W/B ratio.
Keywords: Sodium carbonate, Sodium hydroxide, Hydration heat, Workability, Compressive strength
--------------------------------------------------------------------***--------------------------------------------------------------------
1. INTRODUCTION
Due to the serious environment issues occurring worldwide
in recent years, many efforts have been contributed to reduce
the usage of conventional cement based materials and to
recycle industrial wastes. It is generally accepted that alkali
activated materials (AAM) is considered to be the most
potential product in replacing currently widely used
traditional cement in terms of mechanical properties and
durabilities e.g. fire resistance [1,2] and heavy metal
immobilization [3–7]. Slag has been considered as the most
potential raw material in AAM system, and the relevant
properties and influential factors of slag-based AAM have
been extensively studied from the early stage [8,9]. The
alkali activation of slag involves the dissolution of calcium
and participation of Al to form a C-(A)-S-H type gel [8,9],
promoting the development of high mechanical strength and
durability in AAM systems [10–12].
As a matter of fact, the influence of different alkali activators,
different concentrations and compound alkali activators on
the mechanical properties of AAMs has been extensively
studied. Wang [13] investigated the effect of the type of
alkaline activator, dosage of alkali, the type and fineness of
slag, SiO2/Na2O ratio on the strength of slag-based AAM,
and concluded that waterglass is the best activator in all
cases and the best alkali dosage is within the range of 3.0-5.5%
Na2O by mass of slag. Similar results was obtained by [14],
who used sodium silicate, sodium hydroxide, sodium
carbonate, sodium phosphate and combinations of these
activators to study the influence of activators on the
compressive strengths of Australian slag-based AAM. They
concluded that liquid sodium silicate gave the highest
mechanical strengths followed by sodium carbonate (Na2CO3)
and sodium hydroxide (NaOH) and recommended the
optimum proportion of sodium silicate solution with a
module ratios of 0.75, and 4% Na based on the workability
and compressive strength.
Even though the activating effect of different types of alkali
activator with different concentrations and W/B ratios have
been widely researched, however, only the reaction process
of sodium silicate with slag was systematically studied,
while that of sodium carbonate, in most cases, only behaves
as a reference showing the superiority of sodium silicate. As
a result, actually few researches have been conducted on the
differences of reaction process of sodium carbonate with the
raw material slag compared to other alkali activators. In this
study, the hydration heat of slag activated by sodium
carbonate and sodium hydroxide respectively with the same
related parameters were detected by a calorimeter instrument
to analyze the reaction differences of these two alkali
activators and compare to general AAM and conventional
cement as well. And then, two types of activators (Na2CO3
and NaOH), two different dosages (5% and 7% of equivalent
Na2O by slag weight) and three water to binder ratios (W/B)
(0.37, 0.45 and 0.5) were selected to investigate their
influences on the workability and compressive strength of
slag based AAM.
2. MATERIALS
2.1 Ground Granulated Blast Furnace Slag
The ground granulated blast furnace slag (GGBS) used in
this study was provided by ENCI B.V, the Netherlands, with
the specific surface area of 2998 cm2
/g. Table 1 presents the
chemical composition of the GGBS determined by X-ray
Fluorescence (XRF) and the particle size distribution is
shown in Fig. 1.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 149
Table: 1 Chemical composition of GGBS determined by XRF
Chemical CaO SiO2 Al2O3 Fe2O3 K2O Na2O S-total MgO TiO2 Cl
Component
(wt.%)
38.6 35.5 13.6 0.48 0.48 0.35 1.27 10.2 1.01 0.011
Fig. 1 Particle size distribution of GGBS
2.2 Alkali Activator
The investigated alkali activators were sodium carbonate and
sodium hydroxide (both are in powder form, chemical
analysis level). The powder of alkali activator firstly was
dissolved in water in a 2000 ml glass beaker and then was
put in a sink containing water to cool down for half an hour.
The content of alkali activator and amount of water was
determined by different materials design as shown in Table 2,
while basically the mass of sodium carbonate versus that of
sodium hydroxide equals with the equivalent sodium oxide
(Na2O).
Table: 2 Mix proportions of slag based AAM paste and
related design parameters
Mixture
no.
Activators
W/B
ratio
Content
of
activator
(Na2O %)
Weight of materials /g
Slag Water Activator
1
NaOH
0.37 5%
1200
440 70.99
2
0.45
7%
540
108.38
3 5% 77.44
4 0.5 7% 600 108.38
5
Na2CO3
0.37 5% 440 102.6
6
0.45
5%
540
102.6
7 7% 143.65
8 0.5 5% 600 102.6
The content of activator: equivalent Na2O content of
activator by mass of slag.
3. EXPERIMENT
Table 2 listed the various mixes that were made considering
the different content of alkali activators and water to binder
ratios (W/B). Two types of alkali activator (Na2CO3 and
NaOH), two different dosages (5% and 7% of equivalent
Na2O content by mass of binder) and three different W/B
ratios (0.5, 0.45 and 0.4 respectively), were applied to
compare the relevant materials properties of slag activated by
different alkali activators.
3.1 Heat Release
The heat released from the slag reacted with different types
and content of alkali activators was detected by a calorimetry
instrument (TAM AIR Calorimeter). For hydration heat
experiment, the materials were first mixed in a container and
then poured into a glass of bottle which is then measured in
the calorimeter instrument. As a result, the first procedure of
this experiment would generally takes 4~5 minutes before
measuring the hydration heat of samples.
3.2 Flowability
Following Nematollahi [15] and according to EN 1015-3, the
fresh paste was poured into a Hägermann cone (top diameter
= 70 mm, bottom diameter = 100 mm, height = 50 mm).
Subsequently the top surface of the cone was leveled and the
extra paste was removed. After about 15 seconds the
Hägermann cone was lifted vertically and diameter of the
paste spread was measured along two perpendicular
directions. The relative slump value was derived from the
following equation:
) 1
0
( 2d
p
d
   with 1 2
2
d d
d

 (1)
where p is relative slump, d is the average of two measured
diameters of the paste spread and 0d is bottom diameter of
the conical cone, equals to 100 mm.
3.3 Compressive Strength
To measure the compressive strength of the paste, 8 groups
of specimens (40×40×160 mm3
) were casted in plastic
moulds respectively. To prevent the moisture loss the
molded specimens were sealed with a plastic foil. The
specimens were cured at ambient temperature for 1 day and
then removed from the moulds and cured in water at room
temperature until the age of testing. While in the case of slag
activated by sodium carbonate the specimens could not be
demoulded after 24 h curing because of the slow reaction
rate based on the hydration results. As a result, the specimens
of slag activated with sodium carbonate were removed from
moulds after 3 days of casting. 7-days compression strengths
after casting were measured using a compression machine at
a load rate of 2400 KN/min.
4. RESULTS AND DISCUSSION
4.1 Effect of Activator on the Hydration
The heat release experimental results are shown in Fig. 2. As
can be seen, the reaction process of slag activated by sodium
carbonate and sodium hydroxide is quite different from each
other. According to the conceptual model for reaction
0
5
10
15
20
0.1 1 10 100 1000
Volume(%)
Particle size (Micron)
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 150
processes involved in geopolymerisation suggested by Provis
and Deventer [16,17], the first reaction procedure is the
dissolution (first peak) of raw materials in the alkali solution
followed by the oligomerisation/gelation (second peak),
which are also confirmed by the experiment. The hydration
curve of slag activated with sodium carbonate indicates that
the reaction of the specimens started about 40 hours (second
peak) later than the dissolution (first peak), while the slag
activated with sodium hydroxide started just after the
dissolution part at around 30 minutes. This phenomenon is
confirmed by the compressive strength results. The products
of slag activated with sodium carbonate cannot be
demoulded and remains soft after nearly 2 days curing, while
that of sodium hydroxide can be demoulded after 2 hours
casting, which are correspondence with the heat release
process.
Fig 2 Effect of different types of alkali activators with the
equivalent content of Na2O to the binder on the hydration
heat of specimens at 20 ℃
As a matter of fact, the hydration tendency of both slag
activated by sodium carbonate and sodium hydroxide are
different from that of cement based materials. As shown in
Fig. 3, the hydration heat evaluation rate of different
replacement levels of cement by slag were investigated by
Han [18]. The hydration tendency of cement-slag binder is
similar to that of slag activated with sodium hydroxide but
the period of reaction hump (second hump) of former one
(around 100 hours) is much longer than that of the later one
(about 10 hours). similarly, the delayed setting of slag based
AAM was reported by other authors [14].
Fig 3 Hydration heat evolution rate of cement (CM)
replacing with different contents of slag at 25 ℃[18]
3.2 Flowability
Fig 4. Examples of flow of slag activated by: (Left) Sodium
hydroxide (W/B 0.37 and 5% equivalent Na2O by mass to
the binder/slag), (Right) Sodium carbonate (W/B 0.45 and 7%
equivalent Na2O by mass to the binder/slag)
The relative slump of slag activated with sodium carbonate
and sodium hydroxide is shown in Table 2. As can been seen,
in general, the higher the water content (W/B ratio) the
higher the relative slump will be, which is similar to that of
cement based materials without using superplasticizer. On
the other hand, the higher the alkali content to the binder is,
the lower the relative slump will be. Meanwhile, under the
same equivalent content of Na2O by mass to the binder and
same W/B ratio, the fresh paste of slag activated by sodium
carbonate shows better fluidity than that of sodium
hydroxide. Fig. 4 shows two examples of slump of slag
based AAM paste with different proportions, and the one of
slag activated by sodium carbonate with W/B of 0.45 and 7 %
equivalent Na2O by mass to the binder, while the other one
with 5 % equivalent Na2O and W/B of 0.45 hardly shows
any slump.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 151
Fig 5. Effect of alkali types and contents (Na2O wt.%) and
W/B ratios on the relative slump of slag based AAM paste
(the mixture numbers correlate with Table 2)
3.3 Compressive Strength
Fig. 6 indicates an overview of the influence of alkali types,
alkali content and W/B ratios on the compressive strength of
slag based AAM paste. As can be seen, in general, with an
equivalent content of alkali activator and same W/B ratio, the
slag activated with sodium carbonate shows much better
compressive strength than that of slag reacted with sodium
hydroxide, which is in line with other authors [14]. The
compressive strength of specimens increases with the
decreasing content of water in this alkali activating system,
which is similar to that of cement-based materials. On the
other hand, the compressive strength increases with the
increasing content of alkali activator to the binder, which are
also confirmed others experimental results.
Fig 6. Effect of alkali types and contents (Na2O wt.%) and
W/B ratios on the 7-day compressive strength of slag based
AAM paste
As shown in Fig. 6, the strength tendency of specimens
generally fits with the rules described above. Nevertheless,
the mixture proportions of mixture No.5 (M5) have lower
water content than that of M6 with same Na2O content, while
the strength of M5 is nearly the same as M6. On the other
hand, under an equal W/B ratio, M6 shows a better
compressive strength than that of M7 but with a lower alkali
content. The possible reasons for this phenomenon may lay
on two aspects: 1, water content. A low water content will
cause a poor flowability (Fig. 4), which means air cannot
escape easily from the matrix leading to high porosity. 2, a
high alkali content may increase the viscosity of fresh
reaction product and reduce the workability as well (Fig. 5),
inducing a poor strength.
4. CONCLUSIONS
To conclude, from the perspective of hydration process, it is
apparent that slag activated by sodium carbonate is much
slower than that of sodium hydroxide and conventional
cement-based materials, and slag activated by sodium silicate
[16,17].
1. The reaction process of slag activated with sodium
carbonate is slower than that of those activated with
sodium hydroxide/silicate, and its reaction phase
happens approximately 40 h after the dissolution
phase, indicated by the hydration heat experiment;
2. The slags activated with sodium carbonate shows
better workability than those activated with sodium
hydroxide with the same W/B ratio and Na2O content;
3. The compressive strength of slag activated with
sodium carbonate is much better than that of sodium
hydroxide activated ones;
4. In general, the higher the alkali activator content and
the lower the W/B ratio is, the higher the
compressive strength would be.
REFERENCES
[1]. T. Bakharev, J.. Sanjayan, Y.-B. Cheng, Resistance of
alkali-activated slag concrete to acid attack, Cem. Concr. Res.
33 (2003) 1607–1611.
[2]. E. Prud’homme, P. Michaud, E. Joussein, J.-M. Clacens,
S. Arii-Clacens, I. Sobrados, et al., Structural
characterization of geomaterial foams — Thermal behavior,
J. Non. Cryst. Solids. 357 (2011) 3637–3647.
doi:10.1016/j.jnoncrysol.2011.06.033.
[3]. L. Zheng, C. Wang, W. Wang, Y. Shi, X. Gao,
Immobilization of MSWI fly ash through AAMization:
effects of water-wash., Waste Manag. 31 (2011) 311–7.
[4]. J.Z. Xu, Y.L. Zhou, Q. Chang, H.Q. Qu, Study on the
factors of affecting the immobilization of heavy metals in fly
ash-based AAMs, Mater. Lett. 60 (2006) 820–822.
[5]. J.G.S. Van Jaarsveld, J.S.J. Van Deventer, THE
POTENTIAL USE OF AAMIC MATERIALS TO
IMMOBILISE TOXIC METALS PART I . THEORY AND
APPLICATIONS Best Student Research Paper award for
AAM research , in Australia Amazing World of Science, 10
(1997) 1–10.
[6]. J.L. Provis, P. a. Walls, J.S.J. van Deventer, AAMisation
kinetics. 3. Effects of Cs and Sr salts, Chem. Eng. Sci. 63
(2008) 4480–4489.
[7]. J.W. Phair, J.S.J. van Deventer, J.D. Smith, Effect of Al
source and alkali activation on Pb and Cu immobilisation in
fly-ash based ―AAMs,‖ Appl. Geochemistry. 19 (2004) 423–
434.
[8]. I.G. Richardson, A.R. Brough, G.W. Groves, C.M.
Dobson, Pergamon THE CHARACTERIZATION OF
HARDENED ALKALI-ACTIVATED BLAST-FURNACE
PHASE, 24 (1994) 813–829.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 152
[9]. A.R. Brough, A. Atkinson, Sodium silicate-based ,
alkali-activated slag mortars Part I . Strength , hydration and
microstructure, 32 (2002) 865–879.
[10]. D.M. Roy, W. Jiang, M.R. Silsbee, Chloride diffusion
in ordinary , blended , and alkali-activated cement pastes and
its relation to other properties, 30 (2001).
[11]. T. Bakharev, J.G. Sanjayan, Y.-B. Cheng, Sulfate
attack on alkali-activated slag concrete, Cem. Concr. Res. 32
(2002) 211–216.
[12]. S. a. Bernal, E.D. Rodríguez, R. Mejia de Gutiérrez, J.L.
Provis, S. Delvasto, Activation of Metakaolin/Slag Blends
Using Alkaline Solutions Based on Chemically Modified
Silica Fume and Rice Husk Ash, Waste and Biomass
Valorization. 3 (2011) 99–108.
[13]. S. Wang, K.L. Scrivener, P.L. Pratt, (Communicated by
A.J., 24 (1994) 1033–1043.
[14]. T. Bakharev, J.G. Sanjayan, Y.-B. Cheng, Alkali
activation of Australian slag cements, Cem. Concr. Res. 29
(1999) 113–120.
[15]. B. Nematollahi, J. Sanjayan, Effect of different
superplasticizers and activator combinations on workability
and strength of fly ash based AAM, Mater. Des. 57 (2014)
667–672.
[16]. J.S.J. van Deventer, J.L. Provis, P. Duxson, G.C. Lukey,
Reaction mechanisms in the AAMic conversion of inorganic
waste to useful products., J. Hazard. Mater. 139 (2007) 506–
13.
[17]. J.L. Provis, P. Duxson, J.S.J. Van Deventer, G.C.
Lukey, The Role of Mathematical Modelling and Gel
Chemistry in Advancing AAM Technology, Chem. Eng. Res.
Des. 83 (2005) 853–860..
[18]. F. Han, R. Liu, D. Wang, P. Yan, Characteristics of the
hydration heat evolution of composite binder at different
hydrating temperature, Thermochim. Acta. (2014).
BIOGRAPHIES:
B. Yuan, received his master’s degree from
Wuhan University of Technology, China.
He is currently working as a PhD student in
the Department of Built Environment,
Eindhoven University of Technology.
Q.L. Yu, received his Ph.D. degree from
Eindhoven University of Technology, the
Netherlands. He is currently working as an
assistant professor in the Department of the
Built Environment, Eindhoven University
of Technology.
H.J.H Brouwers is professor Building
Materials and head of the unit Building
Physics & Services at Eindhoven University
of Technology.

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Investigation on the activating effect of na2 co3 and naoh on slag

  • 1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 _______________________________________________________________________________________ Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 148 INVESTIGATION ON THE ACTIVATING EFFECT OF NA2CO3 AND NAOH ON SLAG B. Yuan1 , Q.L. Yu2 , H.J.H Brouwers3 1 Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands 2 Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands 3 Department of Built Environment, Eindhoven University of Technology, Eindhoven, the Netherlands Abstract This study aims to investigate the activating effect of Na2CO3 and NaOH on the workability and mechanic strength of slag-based alkali activated materials with different alkali contents and water to binder ratios. The heat release during the reaction process of slag activated with sodium carbonate and sodium hydroxide were monitored respectively to analyze the hydration process. Meanwhile, the workability and compressive strength were also tested with two types of activators (Na2CO3 and NaOH), two different dosages (5% and 7% of equivalent Na2O by slag weight) and three different water to binder (W/B) ratios (0.37, 0.45 and 0.5). The results show that the reaction process of slag activated with sodium carbonate is much slower than that of sodium hydroxide activated one, and its reaction phase happens approximately 40 h after the dissolution phase, and in all cases, sodium carbonate gives the higher fluidity and compressive strength with the same Na2O content and W/B ratio. Keywords: Sodium carbonate, Sodium hydroxide, Hydration heat, Workability, Compressive strength --------------------------------------------------------------------***-------------------------------------------------------------------- 1. INTRODUCTION Due to the serious environment issues occurring worldwide in recent years, many efforts have been contributed to reduce the usage of conventional cement based materials and to recycle industrial wastes. It is generally accepted that alkali activated materials (AAM) is considered to be the most potential product in replacing currently widely used traditional cement in terms of mechanical properties and durabilities e.g. fire resistance [1,2] and heavy metal immobilization [3–7]. Slag has been considered as the most potential raw material in AAM system, and the relevant properties and influential factors of slag-based AAM have been extensively studied from the early stage [8,9]. The alkali activation of slag involves the dissolution of calcium and participation of Al to form a C-(A)-S-H type gel [8,9], promoting the development of high mechanical strength and durability in AAM systems [10–12]. As a matter of fact, the influence of different alkali activators, different concentrations and compound alkali activators on the mechanical properties of AAMs has been extensively studied. Wang [13] investigated the effect of the type of alkaline activator, dosage of alkali, the type and fineness of slag, SiO2/Na2O ratio on the strength of slag-based AAM, and concluded that waterglass is the best activator in all cases and the best alkali dosage is within the range of 3.0-5.5% Na2O by mass of slag. Similar results was obtained by [14], who used sodium silicate, sodium hydroxide, sodium carbonate, sodium phosphate and combinations of these activators to study the influence of activators on the compressive strengths of Australian slag-based AAM. They concluded that liquid sodium silicate gave the highest mechanical strengths followed by sodium carbonate (Na2CO3) and sodium hydroxide (NaOH) and recommended the optimum proportion of sodium silicate solution with a module ratios of 0.75, and 4% Na based on the workability and compressive strength. Even though the activating effect of different types of alkali activator with different concentrations and W/B ratios have been widely researched, however, only the reaction process of sodium silicate with slag was systematically studied, while that of sodium carbonate, in most cases, only behaves as a reference showing the superiority of sodium silicate. As a result, actually few researches have been conducted on the differences of reaction process of sodium carbonate with the raw material slag compared to other alkali activators. In this study, the hydration heat of slag activated by sodium carbonate and sodium hydroxide respectively with the same related parameters were detected by a calorimeter instrument to analyze the reaction differences of these two alkali activators and compare to general AAM and conventional cement as well. And then, two types of activators (Na2CO3 and NaOH), two different dosages (5% and 7% of equivalent Na2O by slag weight) and three water to binder ratios (W/B) (0.37, 0.45 and 0.5) were selected to investigate their influences on the workability and compressive strength of slag based AAM. 2. MATERIALS 2.1 Ground Granulated Blast Furnace Slag The ground granulated blast furnace slag (GGBS) used in this study was provided by ENCI B.V, the Netherlands, with the specific surface area of 2998 cm2 /g. Table 1 presents the chemical composition of the GGBS determined by X-ray Fluorescence (XRF) and the particle size distribution is shown in Fig. 1.
  • 2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 _______________________________________________________________________________________ Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 149 Table: 1 Chemical composition of GGBS determined by XRF Chemical CaO SiO2 Al2O3 Fe2O3 K2O Na2O S-total MgO TiO2 Cl Component (wt.%) 38.6 35.5 13.6 0.48 0.48 0.35 1.27 10.2 1.01 0.011 Fig. 1 Particle size distribution of GGBS 2.2 Alkali Activator The investigated alkali activators were sodium carbonate and sodium hydroxide (both are in powder form, chemical analysis level). The powder of alkali activator firstly was dissolved in water in a 2000 ml glass beaker and then was put in a sink containing water to cool down for half an hour. The content of alkali activator and amount of water was determined by different materials design as shown in Table 2, while basically the mass of sodium carbonate versus that of sodium hydroxide equals with the equivalent sodium oxide (Na2O). Table: 2 Mix proportions of slag based AAM paste and related design parameters Mixture no. Activators W/B ratio Content of activator (Na2O %) Weight of materials /g Slag Water Activator 1 NaOH 0.37 5% 1200 440 70.99 2 0.45 7% 540 108.38 3 5% 77.44 4 0.5 7% 600 108.38 5 Na2CO3 0.37 5% 440 102.6 6 0.45 5% 540 102.6 7 7% 143.65 8 0.5 5% 600 102.6 The content of activator: equivalent Na2O content of activator by mass of slag. 3. EXPERIMENT Table 2 listed the various mixes that were made considering the different content of alkali activators and water to binder ratios (W/B). Two types of alkali activator (Na2CO3 and NaOH), two different dosages (5% and 7% of equivalent Na2O content by mass of binder) and three different W/B ratios (0.5, 0.45 and 0.4 respectively), were applied to compare the relevant materials properties of slag activated by different alkali activators. 3.1 Heat Release The heat released from the slag reacted with different types and content of alkali activators was detected by a calorimetry instrument (TAM AIR Calorimeter). For hydration heat experiment, the materials were first mixed in a container and then poured into a glass of bottle which is then measured in the calorimeter instrument. As a result, the first procedure of this experiment would generally takes 4~5 minutes before measuring the hydration heat of samples. 3.2 Flowability Following Nematollahi [15] and according to EN 1015-3, the fresh paste was poured into a Hägermann cone (top diameter = 70 mm, bottom diameter = 100 mm, height = 50 mm). Subsequently the top surface of the cone was leveled and the extra paste was removed. After about 15 seconds the Hägermann cone was lifted vertically and diameter of the paste spread was measured along two perpendicular directions. The relative slump value was derived from the following equation: ) 1 0 ( 2d p d    with 1 2 2 d d d   (1) where p is relative slump, d is the average of two measured diameters of the paste spread and 0d is bottom diameter of the conical cone, equals to 100 mm. 3.3 Compressive Strength To measure the compressive strength of the paste, 8 groups of specimens (40×40×160 mm3 ) were casted in plastic moulds respectively. To prevent the moisture loss the molded specimens were sealed with a plastic foil. The specimens were cured at ambient temperature for 1 day and then removed from the moulds and cured in water at room temperature until the age of testing. While in the case of slag activated by sodium carbonate the specimens could not be demoulded after 24 h curing because of the slow reaction rate based on the hydration results. As a result, the specimens of slag activated with sodium carbonate were removed from moulds after 3 days of casting. 7-days compression strengths after casting were measured using a compression machine at a load rate of 2400 KN/min. 4. RESULTS AND DISCUSSION 4.1 Effect of Activator on the Hydration The heat release experimental results are shown in Fig. 2. As can be seen, the reaction process of slag activated by sodium carbonate and sodium hydroxide is quite different from each other. According to the conceptual model for reaction 0 5 10 15 20 0.1 1 10 100 1000 Volume(%) Particle size (Micron)
  • 3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 _______________________________________________________________________________________ Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 150 processes involved in geopolymerisation suggested by Provis and Deventer [16,17], the first reaction procedure is the dissolution (first peak) of raw materials in the alkali solution followed by the oligomerisation/gelation (second peak), which are also confirmed by the experiment. The hydration curve of slag activated with sodium carbonate indicates that the reaction of the specimens started about 40 hours (second peak) later than the dissolution (first peak), while the slag activated with sodium hydroxide started just after the dissolution part at around 30 minutes. This phenomenon is confirmed by the compressive strength results. The products of slag activated with sodium carbonate cannot be demoulded and remains soft after nearly 2 days curing, while that of sodium hydroxide can be demoulded after 2 hours casting, which are correspondence with the heat release process. Fig 2 Effect of different types of alkali activators with the equivalent content of Na2O to the binder on the hydration heat of specimens at 20 ℃ As a matter of fact, the hydration tendency of both slag activated by sodium carbonate and sodium hydroxide are different from that of cement based materials. As shown in Fig. 3, the hydration heat evaluation rate of different replacement levels of cement by slag were investigated by Han [18]. The hydration tendency of cement-slag binder is similar to that of slag activated with sodium hydroxide but the period of reaction hump (second hump) of former one (around 100 hours) is much longer than that of the later one (about 10 hours). similarly, the delayed setting of slag based AAM was reported by other authors [14]. Fig 3 Hydration heat evolution rate of cement (CM) replacing with different contents of slag at 25 ℃[18] 3.2 Flowability Fig 4. Examples of flow of slag activated by: (Left) Sodium hydroxide (W/B 0.37 and 5% equivalent Na2O by mass to the binder/slag), (Right) Sodium carbonate (W/B 0.45 and 7% equivalent Na2O by mass to the binder/slag) The relative slump of slag activated with sodium carbonate and sodium hydroxide is shown in Table 2. As can been seen, in general, the higher the water content (W/B ratio) the higher the relative slump will be, which is similar to that of cement based materials without using superplasticizer. On the other hand, the higher the alkali content to the binder is, the lower the relative slump will be. Meanwhile, under the same equivalent content of Na2O by mass to the binder and same W/B ratio, the fresh paste of slag activated by sodium carbonate shows better fluidity than that of sodium hydroxide. Fig. 4 shows two examples of slump of slag based AAM paste with different proportions, and the one of slag activated by sodium carbonate with W/B of 0.45 and 7 % equivalent Na2O by mass to the binder, while the other one with 5 % equivalent Na2O and W/B of 0.45 hardly shows any slump.
  • 4. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 _______________________________________________________________________________________ Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 151 Fig 5. Effect of alkali types and contents (Na2O wt.%) and W/B ratios on the relative slump of slag based AAM paste (the mixture numbers correlate with Table 2) 3.3 Compressive Strength Fig. 6 indicates an overview of the influence of alkali types, alkali content and W/B ratios on the compressive strength of slag based AAM paste. As can be seen, in general, with an equivalent content of alkali activator and same W/B ratio, the slag activated with sodium carbonate shows much better compressive strength than that of slag reacted with sodium hydroxide, which is in line with other authors [14]. The compressive strength of specimens increases with the decreasing content of water in this alkali activating system, which is similar to that of cement-based materials. On the other hand, the compressive strength increases with the increasing content of alkali activator to the binder, which are also confirmed others experimental results. Fig 6. Effect of alkali types and contents (Na2O wt.%) and W/B ratios on the 7-day compressive strength of slag based AAM paste As shown in Fig. 6, the strength tendency of specimens generally fits with the rules described above. Nevertheless, the mixture proportions of mixture No.5 (M5) have lower water content than that of M6 with same Na2O content, while the strength of M5 is nearly the same as M6. On the other hand, under an equal W/B ratio, M6 shows a better compressive strength than that of M7 but with a lower alkali content. The possible reasons for this phenomenon may lay on two aspects: 1, water content. A low water content will cause a poor flowability (Fig. 4), which means air cannot escape easily from the matrix leading to high porosity. 2, a high alkali content may increase the viscosity of fresh reaction product and reduce the workability as well (Fig. 5), inducing a poor strength. 4. CONCLUSIONS To conclude, from the perspective of hydration process, it is apparent that slag activated by sodium carbonate is much slower than that of sodium hydroxide and conventional cement-based materials, and slag activated by sodium silicate [16,17]. 1. The reaction process of slag activated with sodium carbonate is slower than that of those activated with sodium hydroxide/silicate, and its reaction phase happens approximately 40 h after the dissolution phase, indicated by the hydration heat experiment; 2. The slags activated with sodium carbonate shows better workability than those activated with sodium hydroxide with the same W/B ratio and Na2O content; 3. The compressive strength of slag activated with sodium carbonate is much better than that of sodium hydroxide activated ones; 4. In general, the higher the alkali activator content and the lower the W/B ratio is, the higher the compressive strength would be. REFERENCES [1]. T. Bakharev, J.. Sanjayan, Y.-B. Cheng, Resistance of alkali-activated slag concrete to acid attack, Cem. Concr. Res. 33 (2003) 1607–1611. [2]. E. Prud’homme, P. Michaud, E. Joussein, J.-M. Clacens, S. Arii-Clacens, I. Sobrados, et al., Structural characterization of geomaterial foams — Thermal behavior, J. Non. Cryst. Solids. 357 (2011) 3637–3647. doi:10.1016/j.jnoncrysol.2011.06.033. [3]. L. Zheng, C. Wang, W. Wang, Y. Shi, X. Gao, Immobilization of MSWI fly ash through AAMization: effects of water-wash., Waste Manag. 31 (2011) 311–7. [4]. J.Z. Xu, Y.L. Zhou, Q. Chang, H.Q. Qu, Study on the factors of affecting the immobilization of heavy metals in fly ash-based AAMs, Mater. Lett. 60 (2006) 820–822. [5]. J.G.S. Van Jaarsveld, J.S.J. Van Deventer, THE POTENTIAL USE OF AAMIC MATERIALS TO IMMOBILISE TOXIC METALS PART I . THEORY AND APPLICATIONS Best Student Research Paper award for AAM research , in Australia Amazing World of Science, 10 (1997) 1–10. [6]. J.L. Provis, P. a. Walls, J.S.J. van Deventer, AAMisation kinetics. 3. Effects of Cs and Sr salts, Chem. Eng. Sci. 63 (2008) 4480–4489. [7]. J.W. Phair, J.S.J. van Deventer, J.D. Smith, Effect of Al source and alkali activation on Pb and Cu immobilisation in fly-ash based ―AAMs,‖ Appl. Geochemistry. 19 (2004) 423– 434. [8]. I.G. Richardson, A.R. Brough, G.W. Groves, C.M. Dobson, Pergamon THE CHARACTERIZATION OF HARDENED ALKALI-ACTIVATED BLAST-FURNACE PHASE, 24 (1994) 813–829.
  • 5. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 _______________________________________________________________________________________ Volume: 03 Special Issue: 13 | ICNTCC-2014 | Sep-2014, Available @ http://www.ijret.org 152 [9]. A.R. Brough, A. Atkinson, Sodium silicate-based , alkali-activated slag mortars Part I . Strength , hydration and microstructure, 32 (2002) 865–879. [10]. D.M. Roy, W. Jiang, M.R. Silsbee, Chloride diffusion in ordinary , blended , and alkali-activated cement pastes and its relation to other properties, 30 (2001). [11]. T. Bakharev, J.G. Sanjayan, Y.-B. Cheng, Sulfate attack on alkali-activated slag concrete, Cem. Concr. Res. 32 (2002) 211–216. [12]. S. a. Bernal, E.D. Rodríguez, R. Mejia de Gutiérrez, J.L. Provis, S. Delvasto, Activation of Metakaolin/Slag Blends Using Alkaline Solutions Based on Chemically Modified Silica Fume and Rice Husk Ash, Waste and Biomass Valorization. 3 (2011) 99–108. [13]. S. Wang, K.L. Scrivener, P.L. Pratt, (Communicated by A.J., 24 (1994) 1033–1043. [14]. T. Bakharev, J.G. Sanjayan, Y.-B. Cheng, Alkali activation of Australian slag cements, Cem. Concr. Res. 29 (1999) 113–120. [15]. B. Nematollahi, J. Sanjayan, Effect of different superplasticizers and activator combinations on workability and strength of fly ash based AAM, Mater. Des. 57 (2014) 667–672. [16]. J.S.J. van Deventer, J.L. Provis, P. Duxson, G.C. Lukey, Reaction mechanisms in the AAMic conversion of inorganic waste to useful products., J. Hazard. Mater. 139 (2007) 506– 13. [17]. J.L. Provis, P. Duxson, J.S.J. Van Deventer, G.C. Lukey, The Role of Mathematical Modelling and Gel Chemistry in Advancing AAM Technology, Chem. Eng. Res. Des. 83 (2005) 853–860.. [18]. F. Han, R. Liu, D. Wang, P. Yan, Characteristics of the hydration heat evolution of composite binder at different hydrating temperature, Thermochim. Acta. (2014). BIOGRAPHIES: B. Yuan, received his master’s degree from Wuhan University of Technology, China. He is currently working as a PhD student in the Department of Built Environment, Eindhoven University of Technology. Q.L. Yu, received his Ph.D. degree from Eindhoven University of Technology, the Netherlands. He is currently working as an assistant professor in the Department of the Built Environment, Eindhoven University of Technology. H.J.H Brouwers is professor Building Materials and head of the unit Building Physics & Services at Eindhoven University of Technology.