1. NOVEL CEMENT REPLACEMENT MATERIALS
FOR SUSTAINABLE INFRASTRUCTURE
By
Kingsten Banh
Honors Thesis Defense
Honors Thesis Committee
Dr. Narayanan Neithalath – Dr. Subramaniam Rajan – Dr. Barzin Mobasher
2. INTRODUCTION
Honors Thesis Defense
Every tonne of cement (U.S. Geological Survey, 2009)
→ consumes nearly 4 GJ of energy
→ releases almost one tonne of CO2
• Rapid population growth leads to more demand for cement
→ actively in search for sustainable alternatives
→ merit similar characteristics and properties
• Geopolymer is an intensive area of interest
→ utilized industrial wastes and by-products
→ activated by alkaline solutions
3. GEOPOLYMER – INGREDIENTS
Honors Thesis Defense
Binders Alkali Activators
Aluminosilicates contain high silicon
(Si) and aluminum (Al) oxides.
→ Slags (high calcium)
→ Fly ash
• Class F (low calcium)
• Class C (high calcium)
→ Metakaolin
Activating agents consist of alkali
metal compounds
→ Alkali hydroxides (MOH)
• NaOH
→ Weak acid salts
→ Alkali silicates (M2O∙nSiO2)
• Na2O∙nSiO2
4. Honors Thesis Defense
STRUCTURE OF GEOPOLYMER
Tetrahedral [SiO4]4- and [AlO4]4- anions united by oxygen atoms
Abbreviated as Poly(Sialates) (Davidovits, 2005)
Empirical formula → 𝐌 𝐧 − 𝐒𝐢𝐎 𝟐 𝐳 − 𝐀𝐥𝐎 𝟐 𝐧 ∙ 𝐰𝐇 𝟐 𝐎
Al
SiO
Al
Si
Si
Poly(sialate)
z = 1 (-Si-O-Al-O-)
Poly(sialate-siloxo)
z = 2 (-Si-O-Al-O-Si-O-)
Poly(sialate-disiloxo)
z = 3 (-Si-O-Al-O-Si-O-Si-O-)
Al
Si Si Al
Si
Si
Si
6. PHYSICAL PROPERTIES OF FLY ASH
Honors Thesis Defense
Gray, very fine, and glassy like particles
Particle size between 1 to 100 𝝁m
Regularly shaped particles → cenospheres, plerospheres, and ferrosphers
Irregularly shaped particles → quartz, unburned coal particles
cenosphere plerosphere ferrosphere diatomite
Komljenovi, 2010
7. ACTIVATOR PARAMETERS
Honors Thesis Defense
Sodium hydroxide (NaOH)
→ varying the molarity concentration
Sodium silicates
→ n = Na2O/Binder
→ Ms = Silica modulus = moles of SiO2/moles of Na2O
Liquid sodium silicate (waterglass) with Ms = 3.26
Ms value needs to be reduced to increase the alkali content
8. GEOPOLYMER – INGREDIENTS
Honors Thesis Defense
Binder
– Class F fly ash (ASTM C 618)
→ 100% fly ash
→ liquid/powder = 0.40
Alkali activators
– Sodium hydroxide (NaOH)
→ 4 M and 8 M
– Liquid sodium silicates (Waterglass)
→ n-values of 0.04 and 0.07
→ Ms-values of 2.0 and 1.0
sodium hydroxide
waterglass
10. EXPERIMENTAL PROGRAMS
Honors Thesis Defense
Compressive strength
• 50 mm size cubical mortars – 6 cubes per matrix
• cured 40oC, 60oC, and 80oC
• under dry or moist heat curing condition
• duration of 24 and 72 hours
Factorial statistical analysis
• to evaluate the effects of investigating factors
• to determine the most influential factor(s)
11. COMPRESSIVE STRENGTH TEST
Honors Thesis Defense
• in compliance with ASTM C109 Standard
• 6 cubes per matrix
• allow to the samples to cool down to ambient temperature
before performing the test
15. Honors Thesis Defense
ECONOMIC EFFICIENCY OF
ALKALI ACTIVATORS
To determine how much energy consumed per MPa
of compressive strength
𝐸𝑓𝑓𝑖𝑐𝑖𝑒𝑛𝑡 =
𝐸𝑛𝑒𝑟𝑔𝑦 𝐶𝑜𝑛𝑠𝑢𝑚𝑡𝑖𝑜𝑛
𝑀𝑃𝑎
=
𝑘𝑊
𝑀𝑃𝑎
16. Honors Thesis Defense
ENERGY USAGE AND ASSUMPTION
Power Usage
𝑃 = 𝑅 × 𝐼2
Resistivity
𝑅(𝑇) = 𝑅 𝑜[1 + 𝛼 𝑇 − 𝑇𝑜 ]
P = Power usage
R = Resistance
I = Current
Ro = initial resistance
R(T)= temperature dependent resistance
To = initial temperature
T = final temperature
𝛼 = temperature coefficient
17. Honors Thesis Defense
ASSUMPTIONS & CALCULATIONS
Resistivity
Due to the lack of manufacture information
Simplicity of calculation
→ 𝑹 𝒐 = 𝟏 𝜴 → 𝜶 = 𝟏 → 𝑻 𝒐 = 𝟐𝟑 𝒐 𝑪
𝑹 𝑻 = 𝑹 𝒐[𝟏 + 𝜶 𝑻 − 𝑻 𝒐 ]
At T = 40OC, R = 1[1+1(40 – 23)] → 𝑹 𝟒𝟎 𝒐 𝑪 = 𝟏𝟖 𝜴
At T = 60OC, R = 1[1+1(60 – 23)] → 𝑹 𝟔𝟎 𝒐 𝑪 = 𝟑𝟖 𝜴
At T = 80OC, R = 1[1+1(80 – 23)] → 𝑹 𝟔𝟎 𝒐
𝑪 = 𝟓𝟖 𝜴
18. Honors Thesis Defense
ASSUMPTIONS & CALCULATIONS
Power Consumption – assuming current, I = 5 A
𝑷 = 𝑹 × 𝑰 𝟐
Temperature Resistance
Power consumption, kWh
1 Hour 24 Hours 72 Hours
40 18 0.45 10.8 32.4
60 38 0.95 22.8 68.4
80 58 1.45 34.8 104.4
22. SUMMARY OF INFLUENCE OF THE
INVESTIGATING FACTORS
Honors Thesis Defense
NaOH
Similarities
Low strength development at low temperature and early age
Higher strength as temperature increases and under moist curing
Higher strength → energy consumption
Differences Waterglass
→ significant difference between moist and dry curing √
→ demonstrated higher compressive strength √
→ lowest energy per MPa of compressive stress 8M
(24 & 72 hours)
Ms= 1.0
(24 hours)
23. 2K FACTORIAL DESIGN
Honors Thesis Defense
To evaluate the influence of the investigating factors and
optimize the compressive strength
25-1 – One-half factorial design (A, B, C, E)
Factors Description
Low level
(-1)
High level
(+1)
A Ms 2 1
B n 0.04 0.07
C Curing condition Dry Moist
D Temperature 60 80
E Alumina 0.1 0.2
Objective
Useful when there are several variables in the systems
24. 24 FACTORIAL DESIGN
Honors Thesis Defense
Run
#
Treatment
Combination
Main Effect
A B C D
1 (1) -1 -1 -1 -1
2 a 1 -1 -1 -1
3 b -1 1 -1 -1
4 ab 1 1 -1 -1
5 c -1 -1 1 -1
6 ac 1 -1 1 -1
7 bc -1 1 1 -1
8 abc 1 1 1 -1
… … … … … …
16 abcd 1 1 1 1
25. 24 FACTORIAL DESIGN
Honors Thesis Defense
Categories Model Term
Main Effects A B C D
Two-factor Interactions
AB AC AD
BC BD
CD
Three-factor Interactions
ABC ABD
BCD
26. 25-1 ONE-HALF FACTORIAL DESIGN
Honors Thesis Defense
Run
#
Treatment
Combinati
on
Main Effect Generator
A B C D E
1 e -1 -1 -1 -1 1
2 a 1 -1 -1 -1 -1
3 b -1 1 -1 -1 -1
4 abe 1 1 -1 -1 1
5 c -1 -1 1 -1 -1
6 ace 1 -1 1 -1 1
7 bce -1 1 1 -1 1
8 abc 1 1 1 -1 -1
… d … … … … …
16 ade 1 1 1 1 1
27. Honors Thesis Defense
Initial Regression Model
𝒚 = 𝜷 𝟎 + 𝜷 𝟏 𝒙 𝟏 + 𝜷 𝟐 𝒙 𝟐 + 𝜷 𝟑 𝒙 𝟑 + 𝜷 𝟒 𝒙 𝟒 + 𝜷 𝟓 𝒙 𝟓 + 𝜷 𝟏𝟐 𝒙 𝟏 𝒙 𝟐 + ⋯ + 𝜷 𝟏𝟐𝟑𝟒𝟓 𝒙 𝟏 𝒙 𝟐 𝒙 𝟑 𝒙 𝟒 𝒙 𝟓
25-1 ONE-HALF FACTORIAL DESIGN
Defining relation – 𝑰 = 𝑨𝑩𝑪𝑫𝑬
Aliases
Main Effects
A = BCDE B = ACDE C = ABDE D = ABCE E = ABCD
Interaction Effects
AB = CDE AC = BDE AD = BCE AE = BCD
CD = ABE CE = ABD DE = ABC
BC = ADE BD = ACE BE = ACD
28. 25-1 ONE-HALF FACTORIAL DESIGN
Honors Thesis Defense
Run #
Treatment
Combination
Main Effect Generator Response
A B C D E
24
Hours
72
Hours
1 e -1 -1 -1 -1 1 8.40 10.14
2 a 1 -1 -1 -1 -1 3.26 4.00
3 b -1 1 -1 -1 -1 22.84 25.14
4 abe 1 1 -1 -1 1 17.83 20.74
5 c -1 -1 1 -1 -1 10.20 11.99
6 ace 1 -1 1 -1 1 5.56 6.80
7 bce -1 1 1 -1 1 26.67 28.91
8 abc 1 1 1 -1 -1 22.98 24.59
… d … … … … … … …
16 ade 1 1 1 1 1 31.78 33.48
29. ANALYSIS OF VARIANCE
Honors Thesis Defense
24 Hours 72 Hours
Model
Term
Effect
Estimate
SS % Contribution
Effect
Estimate
SS % Contribution
A -0.54 1.15 0.07 -0.84 2.86 0.16
B 19.01 1446.09 88.84 20.26 1642.54 89.54
C 2.33 21.77 1.34 2.23 19.87 1.08
D 2.43 23.57 1.45 2.40 23.03 1.26
E -0.31 0.37 0.02 -0.20 0.17 0.01
AB 1.14 5.22 0.32 0.82 2.69 0.15
AC -0.44 0.76 0.05 -0.84 2.79 0.15
AD 4.09 66.75 4.10 4.17 69.48 3.79
AE 0.27 0.29 0.02 0.64 1.62 0.09
BC 1.49 8.86 0.54 1.38 7.61 0.42
BD 3.29 43.20 2.65 3.65 53.39 2.91
BE -0.89 3.16 0.19 -1.09 4.79 0.26
CD -0.94 3.50 0.21 -0.84 2.82 0.15
CE 0.87 3.03 0.19 0.17 0.12 0.01
DE -0.10 0.04 0.00 -0.42 0.71 0.04
SSTotal 1627.77 SSTotal 1834.47
30. ANALYSIS OF VARIANCE (24 HOURS)
Honors Thesis Defense
Source Effect Estimate SS DF Mean Square F value f(𝜶, n, d)
Prob >
F
Model - 1601.38 5 320.27 121.40 0.05,5,10 3.71 0.0000
B 19.01 1446.09 1 1446.09 548.14 0.05,1,10 4.96 0.0000
C 2.33 21.77 1 21.77 8.25 0.05,1,10 4.96 0.0167
D 2.43 23.57 1 23.57 8.93 0.05,1,10 4.96 0.0137
AD 4.09 66.75 1 66.75 25.30 0.05,1,10 4.96 0.0005
BD 3.29 43.20 1 43.20 16.37 0.05,1,10 4.96 0.0023
Residual 26.38 10 2.64
SSTotal 1627.77 15 R2 0.984 Adj R2
Final Regression Model
𝒚 = 𝟏𝟓. 𝟗𝟑 + 𝟗. 𝟓𝟏𝒙 𝟐 + 𝟏. 𝟏𝟕𝒙 𝟑 + 𝟏. 𝟐𝟏𝒙 𝟒 + 𝟐. 𝟎𝟒𝒙 𝟏 𝒙 𝟒 + 𝟏. 𝟔𝟒𝒙 𝟐 𝒙 𝟒
32. ANALYSIS OF VARIANCE (24 HOURS)
Honors Thesis Defense
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
B - Ms Values
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
C - Curing Conditions
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
D - Temperature
To increase compressive strength
B at high level
C can be at either low or high
D can be at either low or high
33. ANALYSIS OF VARIANCE (24 HOURS)
Honors Thesis Defense
0
5
10
15
20
25
30
Low High
CompressiveStress,MPa
B - n values
D- D+
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
A - Ms value
D- D+
A and D should be at high level B and D should be at high level
34. ANALYSIS OF VARIANCE (72 HOURS)
Honors Thesis Defense
Source Effect Estimate SS DF Mean Square F value f(𝜶, n, d)
Prob >
F
Model 1808.31 5 361.66 138.24 0.05,5,10 3.71 0.00000
B 20.2641 1642.54 1 1642.53 627.88 0.05,1,10 4.96 0.00000
C 2.22859 19.87 1 19.86 7.59 0.05,1,10 4.96 0.02028
D 2.39952 23.03 1 23.03 8.80 0.05,1,10 4.96 0.01412
AD 4.16774 69.48 1 69.48 26.55 0.05,1,10 4.96 0.00043
BD 3.6535 53.39 1 53.39 20.40 0.05,1,10 4.96 0.00111
Residual 26.16 10 2.62
SSTotal 1834.47 15 R2 0.986 Adj R2
Final Regression Model
𝒚 = 𝟏𝟕. 𝟕𝟒 + 𝟏𝟎. 𝟏𝟑𝒙 𝟐 + 𝟏. 𝟏𝟏𝒙 𝟑 + 𝟏. 𝟐𝟎𝒙 𝟒 + 𝟐. 𝟎𝟖𝒙 𝟏 𝒙 𝟒 + 𝟏. 𝟖𝟑𝒙 𝟐 𝒙 𝟒
36. ANALYSIS OF VARIANCE (72 HOURS)
Honors Thesis Defense
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
B - Ms Values
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
C - Curing Conditions
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
D - Temperature
To increase compressive strength
B at high level
C can be at either low or high
D can be at either low or high
37. ANALYSIS OF VARIANCE (72 HOURS)
Honors Thesis Defense
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
A - Ms value
D- D+
0
5
10
15
20
25
30
35
Low High
CompressiveStress,MPa
B - n values
D- D+
A and D should be at low level B and D should be at high level
38. CONCLUSION
Honors Thesis Defense
• Sodium hydroxide activated fly ash mortars demonstrated
higher compressive strength.
• 8M NaOH activated systems and Ms of 1.0 provides the
most efficient usage of energy
• Factorial design assists in design the experiment runs
• Na2O/binder ratio, n, is the most influential factors to the
compressive strength of waterglass activated systems
The production of cement is energy intensive and causing environment impact.
For every tonne of cement, about 4 GJ of energy is consumed and one tonne of CO2 is released.
With a rapid population growth, the demand for cement is increasing and reaching nearly 3 Gtonnes annually according to U.S Geological survey in 2009.
To reduce both energy consumption and greenhouse gas emissions, the cement industry is under pressure to search for sustainable alternatives that merit similar characteristics and mechanical properties.
For decades of research, geopolymer consists of alkali-activated aluminosilicates materials has been developed and refined to obtain a better understanding of the materials.
So what ingredients are used to make geopolymer ?
The two main ingredients involve in the formation of geopolymer are the aluminosilicate binder and alkali activating agent.
The binders are composed of high aluminosilicates contain such as slags and fly ash, while the alkaline activating agents are compounds of alkali metals.
For the scope of this thesis, class F fly ash was activated by various concentration of sodium hydroxide and liquid sodium silicates solutions.
The structure of geopolymer is composed of tetrahedral negatively charge [SiO4]4- and [AlO4]4- connected by the oxygen ions in which is named “poly(sialates)”.
The word “poly” means many, and “sialate” is an abbreaviation for silicon-oxo-aluminate.
Due to the presense of negatively charged Al in the 4-fold coordination, dissolution of alkali metal compounds will provide a positive cation to balance out the charge. The reaction product of the geopolymer is quite complex, but it has been simplified in this empirical formula
accounting for the main components, where M is a cation from alkali metal compound, n is the degree of polycondensation, and z is commonly known as 1, 2, and 3. to indicate the numbers of [SiO4]4- present in the compound.
At z = 1, one [SiO4]4- connects to [AlO4]4-. At z = 2, two [SiO4]4- connects to [AlO4]4- , and so on.
Different aluminosilicate-based materials produces different geopolymer properties and microstructure as well as different reaction mechanism.
Solid aluminosilicate particles is being attacked by the alkali species in the system.
At high pH level, the amorphous aluminosilicates dissolve very rapidly and quickly reach the equilibrium state.
In this supersaturated aluminosilicate solution, the formation of gel creates larger networks by condensation and release water that was consumed during the dissolution.
The system continue to rearrange and reorganize as the connectivity of the gel increases resulting in the three-dimensional aluminosilicate network
The structural reorganization determine the microstructure and pore distribution of the materials that governs many physical properties of the materials.
Now, let’s take a look at the formation and physical properties of typical fly ash.
At high temperature and pressure, the combustion of coal in power stations produces different types of ash depending on the constituent within the coals.
While the organic matter and carbon are evaporated, many mineral impurities such as clays and quartz melt at high temperature.
The resulting molten impurities quickly transported to the low-temperature zones to solidify into fine, gray, and glass particles of ash
Although fly ash appears as homogenous materials within human eyes, it is indeed a heterogeneous material comprising particles of different dimension various shapes.
Cenosphere is light and hallow sphere made of silica and alumina that filled with air.
Plerosphere is a large sphere covering smaller particles inside
Ferrosphere has a rough surface
Figure A present together with the unreacted spheres (point 3) along with the existing amorphous aluminosilicate gel (points 4 and 5).
The considerable amount of unreacted or not totally consumed spheres is indicating a moderate degree of reaction in the system.
Point 6 of Figure B show the main matrix of reaction product and some deposits of crystalline material. In Figure C, some fly ash spheres partially covered with reaction product as indicated by the arrows.
This picture might be suggesting that the precipitation of the reaction products forms out of the supersaturated dissolution of aluminosilicate.
This fact could justify the moderate degree of reaction already taken place in this type of systems.
Finally, Figure D indicates that the interfacial area between the aggregate and the aluminosilicate gel matrix is almost non-existent which could mean that the adherence of the cementitious material with the aggregates is really good.
Two different alkali activators are used to activate the formation of geopolymer.
For sodium hydroxide, various molarity concentration of the solution will be used.
On another hand, two different activator parameters for liquid sodium silicates. “n” indicates the sodium dioxide-to-binder ratio and “Ms” is the Silicon dioxide-to-sodium dioxide ratio.
Since the moles ratio of the Ms (60/62) is 0.97 which can be assumed to be 1:1 ratio. So, every 1,000 g of fly ash having a n-value of 0.05 and Ms-value of 1.0 requires a total of 50 g of Sodium dioxide and 50 g silicon dioxide.
Ultimately, the Ms and n values are additional alkali solution and soluble silicate that will be added to the systems.
For the investigation within the thesis, class F fly ash conforming ASTC C 618 was used as the sole binding material in the formation of geopolymers.
4M and 8M concentration of sodium hydroxide solutions with a liquid to binder ratio of 0.4 were prepared to activate the binder.
On another hand, liquid sodium silicates or waterglass with n-values of 0.04 and 0.07 along with MS values of 2.0 and 1.0 were used to activate the binder for another study in this thesis.
Although there are two different alkali activators, the mixing procedures are very similar.
If the activator is sodium hydroxide, NaOH salt is mixed with the required amount of water to achieve the desired molarity.
For Waterglass as the activating agent, the desired Ms value is often smaller then the one from the actual waterglass.
So, additional NaOH solution is required to add into the waterglass solution to bring the value down.
Because both activators are composed of sodium, the dissolution of each activators with water is exothermal in which heat is released.
Therefore, the solutions require about 2 to 3 hours to cool down to the ambient temperature. Prior mixing the solution with binder, the required amount of fly ash and sand are first dry mixed together for two minutes to prevent the formation of clump when the liquid is added.
Then, the solution is added into the binders and further mixed for another three minutes until obtain a uniform mixture.
\
As it can be observed in the figures, the highest compressive strength are reached at 8M activator concentration. In early age, the compressive strength development of the mixtures were equal or slightly higher at very low temperature regardless the concentration of NaOH solutions.
Moist heat curing provides higher compressive strength over convectional dry curing, the effect was not as much as the effect of curing temperature and the concentration of NaOH. Under moist heat curing, the samples are surrounded by high relative humidity compared to dry heat curing in which will prevent the occurrence of carbonation that will lower the pH level and lead to a reduction in reaction rate.
At 24 hours curing, the higher concentration of NaOH shows a boost in compressive strength from 4M to 8M, but not as much when compared to the increase of strength due to the increase of NaOH concentration for 72 hours cured samples. When more curing time was allowed, the newly formed aluminosilicate network had more “time” rearranging and reorganizing by utilizing the available sodium cations in the system to form a more complex and stronger network. The compressive strength of this set of data reached about 50 MPa at 80oC under moist curing for three days. The lowest strength occurred below 5 MPa for 24 hours at 40oC regardless the NaOH concentrations.
Now, let’s investigate how the compressive strength be influenced by the silica modulus, Na2O/binder ratio, and the curing parameters (conditions, durations, and temperatures).
Effect of curing condition
Early age – regardless anything
Ms value – high value -> lower strength
N value – high value -> higher strength
Temperature – increase -> increase strength
Max and min compressive strength
Curing duration
Similar for the Ms of 1.0, at low temperature and early age, there are also not a distinguishable difference between the compressive stress of the mixtures.
But as temperature, high concentration of Na2O in the systems favor the mechanical strength development of the samples.
At Ms of 1 and n of 0.07, as temperature increases, there is a huge difference in compressive strength of moist cured samples compared dried cured.
On another hand, at Ms of 1 and n of 0.04, the difference between moist and dry curing is not very significant.
This set of data also shows similar trends obtained from previous slide. The lowest strength development at low temperature and early age in which the compressive stress is about 10 ± 3 MPa. The highest compressive stress can be obtained from moist cured sample at Ms = 1 and n = 0.07, which is about 35 MPa.