Cement Chemistry and Advanced Binder SystemsIntroduction and ContextCement is the chemically active component of most concrete and mortar systems. Although concrete performance is often discussed in terms of water–cement ratio, strength, workability and durability, these engineering properties originate in reactions occurring at the scale of nanometres to millimetres. Cement manufacture determines clinker mineralogy; mineralogy controls hydration; hydration produces a progressively refined pore structure; and pore structure governs transport, strength, shrinkage and durability. Contemporary construction additionally requires binders with lower embodied carbon, improved resistance to aggressive environments and reliable performance when industrial by-products or alternative raw materials are used. Portland cement therefore needs to be understood both as a conventional material and as one member of a broader family of cementitious systems that includes blended cements, alkali-activated binders, geopolymers and calcium sulfoaluminate-based cements. This chapter develops the chemistry and engineering implications of these systems. Chemical notation used in cement science is abbreviated: C = CaO, S = SiO₂, A = Al₂O₃, F = Fe₂O₃, H = H₂O and $\bar{S}$ = SO₃. Thus, C₃S denotes approximately 3CaO·SiO₂. Learning ObjectivesBy the end of this chapter, the reader should be able to: 1. Explain the principal stages of Portland cement manufacture and the functions of clinker phases. 2. Describe the mechanisms and products of cement hydration. 3. Relate pore structure and heat evolution to strength, permeability and durability. 4. Evaluate supplementary cementitious materials and chemical admixtures. 5. Compare Portland, blended, alkali-activated, geopolymer and low-carbon binder systems. 6. Select and assess binder systems using performance, sustainability, constructability and governance criteria. 1. Manufacture and Composition of Portland Cement1.1 Raw materials and process stagesThe principal raw materials are limestone, supplying calcium carbonate, and clay, shale or other siliceous and aluminous materials. Corrective materials may supply iron, silica or alumina. The manufacturing sequence is: 1. quarrying and crushing; 2. proportioning and grinding of raw materials; 3. homogenisation of raw meal; 4. preheating and precalcination; 5. rotary-kiln burning and clinker formation; 6. cooling of clinker; and 7. finish grinding with gypsum and, where permitted, other constituents. The dominant calcination reaction is: CaCO₃ → CaO + CO₂. This reaction is both chemically essential and a major source of greenhouse-gas emissions. Additional emissions arise from kiln fuel and electricity. In the kiln, temperatures commonly approach 1450 °C in the burning zone. Rapid clinker cooling is important because it helps preserve reactive, desirable phase assemblages and limits excessive crystal growth. Gypsum is interground with clinker primarily to regulate setting. Without sulfate control, the highly reactive aluminate phase can react rapidly with water, causing flash set. 1.2 Principal clinker phasesThe main phases are: - Tricalcium silicate (C₃S): hydrates relatively rapidly and is chiefly associated with early strength and substantial heat release.
- Dicalcium silicate (C₂S): hydrates more slowly and contributes significantly to later-age strength. The β form is particularly important in ordinary clinker.
- Tricalcium aluminate (C₃A): reacts very rapidly and strongly with sulfate; it influences setting, early heat and sulfate resistance.
- Tetracalcium aluminoferrite (C₄AF): contributes less to strength than the silicates and affects colour, burnability and liquid formation in the kiln.
Actual clinker contains solid solutions, alkalis, magnesium, sulfate and minor phases. Consequently, phase calculations based on oxide composition are estimates rather than direct measurements. The Bogue equations are useful for approximate phase estimation from bulk oxide analysis, but they assume equilibrium phase relationships and do not fully represent modern clinker microstructures. X-ray diffraction with quantitative analysis, microscopy and calorimetry provide more reliable assessment. 1.3 Manufacture-related quality variablesImportant variables include raw meal fineness, kiln temperature profile, residence time, clinker cooling rate, sulfate balance, clinker alkali content and cement fineness. Finer cement generally hydrates more rapidly because of increased surface area, but it may increase water demand, early heat and shrinkage. Excessive or poorly balanced sulfate can cause abnormal setting or later expansion. Quality control should therefore combine chemical analysis with tests of setting time, soundness, fineness, strength and heat evolution. 2. Hydration Chemistry and Microstructure2.1 Stages of hydrationWhen water contacts cement, dissolution begins at particle surfaces. Ions enter solution, followed by nucleation and growth of hydration products. Heat-flow calorimetry commonly identifies five overlapping periods: 1. Initial reaction: rapid wetting, dissolution and early formation of hydrates. 2. Dormant or induction period: comparatively low heat flow, allowing mixing, transport and placement. 3. Acceleration period: rapid precipitation of calcium–silicate–hydrate and portlandite, associated with setting and early strength. 4. Deceleration period: reaction becomes limited by product layers, diffusion and declining reactant availability. 5. Long-term reaction: slow hydration of remaining particles and continued microstructural development. The boundaries are not fixed. They change with temperature, fineness, water content, admixtures, sulfate availability and supplementary cementitious materials. 2.2 Silicate hydrationA simplified representation of alite hydration is: 2C₃S + 6H → C₃S₂H₃ + 3CH. For belite, a simplified expression is: 2C₂S + 4H → C₃S₂H₃ + CH. Here, C₃S₂H₃ represents calcium–silicate–hydrate, conventionally abbreviated C–S–H, and CH represents calcium hydroxide, or portlandite. The stoichiometry of C–S–H is variable; it is not a single pure compound. C–S–H is the principal binding phase and commonly has a calcium-to-silicon ratio lower than that of the original silicate phases. It forms a poorly crystalline, gel-like assemblage with nanoscale pores and variable incorporated ions. C₃S generally reacts faster than C₂S. This distinction explains why increasing the proportion of C₃S tends to increase early strength and heat, whereas C₂S-rich cements may develop strength more slowly but can offer lower heat evolution. 2.3 Aluminate and sulfate reactionsIn the presence of gypsum, C₃A initially forms ettringite, often represented as AFt (aluminate–ferrite–trisulfate), which helps control setting. If sulfate becomes depleted, AFt may partially convert to monosulfate, an AFm phase. Simplified reactions cannot capture the full range of substitutions involving carbonate, iron, alkalis and magnesium. The balance between aluminate reactivity and available sulfate is critical. Insufficient sulfate can cause rapid stiffening, while excessive sulfate or incompatible chemical conditions may contribute to delayed expansion or abnormal setting. Sulfate resistance is influenced not only by C₃A content but also by permeability, curing, pore solution chemistry and the presence of reactive alumina in blended systems. 2.4 Hydration products and interfacial zonesThe main products are C–S–H, portlandite, AFt, AFm and residual unhydrated clinker. C–S–H provides most of the solid bonding and strength. Portlandite contributes alkalinity but is relatively soluble and less effective than C–S–H in resisting mechanical damage. In concrete, the interfacial transition zone around aggregate particles may initially contain more porosity and oriented portlandite crystals than the bulk paste. Silica fume, fine mineral additions and adequate curing can reduce this contrast through filler effects and pozzolanic reaction. 3. Pore Structure, Strength and Transport3.1 Types of poresCement paste contains several overlapping pore populations: - gel pores within or between C–S–H domains;
- capillary pores left by spaces initially occupied by water and not filled by hydration products;
- entrained-air voids, intentionally introduced and relatively uniform in a well-designed air-entrained system; and
- entrapped-air voids, larger irregular voids caused by inadequate consolidation.
The total porosity is less important than pore-size distribution, connectivity and tortuosity. A paste may contain substantial isolated gel porosity but still have low permeability. Conversely, a smaller volume of connected capillary pores can dominate transport. 3.2 Water–cement ratio and degree of hydrationAt a fixed curing regime, reducing the water–cement ratio generally reduces capillary porosity, provided the mixture remains adequately compacted and hydrated. However, very low water contents can leave unhydrated cement and cause self-desiccation. Autogenous shrinkage and internal relative-humidity loss may then become important. A useful conceptual relationship is Powers’ model, in which capillary porosity decreases as hydration products occupy the original water-filled space. The model is valuable for interpretation, but its assumptions of uniform hydration and idealised volumes limit direct prediction for modern blended or internally cured systems. Strength is governed by the volume, continuity and quality of the solid skeleton, not by water–cement ratio alone. Curing temperature, age, mineral additions, air content, aggregate restraint and defects also matter. Permeability is especially sensitive to connected capillary porosity and cracking. 3.3 Transport and durabilityChloride ingress, carbonation, sulfate solution ingress and moisture movement occur through combinations of diffusion, capillary suction, permeation and ionic interaction. Effective transport coefficients depend on saturation, temperature, binding, cracking and exposure history. A refined pore structure usually lowers transport, but carbonation may proceed faster in some low-calcium blended systems because reduced portlandite reserve lowers buffering capacity. Durability design must therefore evaluate the specific exposure mechanism rather than assume that every blended cement behaves identically. 4. Heat Evolution and Thermal ManagementHydration is exothermic. The total heat released depends on cement composition, degree of hydration and mixture constituents, while the rate depends on fineness, temperature, admixtures and curing conditions. Heat-flow calorimetry reports heat flow as a function of time and cumulative heat per unit mass of binder. In a large concrete element, heat generated internally may not dissipate rapidly. Temperature rises during hydration and is followed by cooling. If the temperature difference between the interior and surface becomes excessive, thermal tensile stresses may exceed the developing tensile strength, producing cracking. Thermal cracking risk is therefore a coupled problem involving heat generation, thermal conductivity, restraint, elastic modulus, creep, tensile strength and environmental cooling. A simplified adiabatic temperature estimate is: ΔT = Q/(ρc), where ΔT is temperature rise, Q is heat released per unit volume, ρ is concrete density and c is specific heat capacity. This equation assumes adiabatic conditions, uniform temperature and no heat loss. It is a screening estimate, not a substitute for a transient heat-transfer and stress analysis. Thermal-control measures include low-heat or blended cement, reduced binder content, staged placement, precooling, insulation, post-cooling, adequate curing and temperature monitoring. Replacing part of Portland clinker with slag, fly ash or calcined clay commonly reduces early heat, although the outcome depends on replacement level, fineness, activators and curing temperature. 5. Supplementary Cementitious MaterialsSupplementary cementitious materials (SCMs) are finely divided materials that contribute through hydraulic reaction, pozzolanic reaction, filler action or combinations of these mechanisms. 5.1 Fly ashClass F fly ash is generally low in calcium and predominantly pozzolanic; Class C fly ash usually contains more calcium and may possess self-cementing behaviour. Fly ash can improve workability, reduce heat and enhance later-age strength and chloride resistance. Potential limitations include slower early strength, variability in carbon content, sensitivity to curing temperature and possible interaction with admixtures. 5.2 Ground granulated blast-furnace slagSlag is a latent hydraulic material. In alkaline, calcium-rich cement pore solution it reacts to form C–S–H-like and other calcium aluminosilicate hydrates. Slag commonly reduces permeability and heat and may improve resistance to chloride ingress. High replacement levels can reduce early strength under cool curing and may increase carbonation sensitivity if curing is poor. 5.3 Silica fumeSilica fume is extremely fine and rich in amorphous silica. It reacts rapidly with portlandite and provides a powerful filler effect, producing very low permeability and high strength when dispersion and curing are adequate. It increases water demand and can increase plastic shrinkage; a high-range water reducer is normally required. 5.4 Metakaolin and calcined claysCalcined kaolinitic clay, including metakaolin, is highly reactive because dehydroxylation produces an amorphous aluminosilicate. It can increase early strength, refine pores and consume portlandite. More broadly, calcined low-grade clays are attractive because clay resources are widespread and calcination temperatures may be lower than those used for clinker production. Their performance depends on mineralogy, calcination control, fineness and sulfate balance. 5.5 Limestone and filler materialsLimestone can act as a physical filler and can participate in carboaluminate formation in aluminate-bearing systems. It may improve particle packing and reduce clinker content. The permitted composition and performance requirements are governed by applicable standards. SCM selection should be based on demonstrated performance, not carbon reduction alone. 6. Chemical AdmixturesChemical admixtures are added in small quantities to modify fresh or hardened properties. - Water reducers and superplasticisers improve flow at a given water content. Polycarboxylate ether systems disperse particles through electrostatic and steric mechanisms.
- Set retarders extend working time, useful in hot weather or long transport, but overdosing can cause severe delay.
- Accelerators increase early reaction, particularly in cold conditions. Chloride-bearing accelerators are restricted or prohibited in reinforced and prestressed concrete because of corrosion risk.
- Air-entraining agents create stable microscopic air voids that improve freeze–thaw resistance. Excess air reduces strength.
- Viscosity-modifying agents reduce segregation and are useful in self-compacting concrete.
- Shrinkage-reducing admixtures lower capillary tension effects but may influence strength and setting.
- Corrosion inhibitors alter electrochemical conditions or reduce corrosion rate, but they are not a substitute for adequate cover and low permeability.
Admixture compatibility must be verified with the actual cement, SCMs, water quality, temperature and mixing procedure. The correct dosage is a performance-based outcome of laboratory and field trials, not a universal percentage. 7. Alkali-Activated Binders and Geopolymers7.1 Alkali-activated bindersAn alkali-activated binder is produced by reacting an aluminosilicate or calcium-rich precursor with an alkaline activator. Precursors include slag, fly ash, calcined clay and combinations of these materials. Activators may be hydroxides, silicates, carbonates or blended alkaline solutions. Reaction involves dissolution of reactive silica and alumina, transport of species and precipitation or polymerisation into binding gels. Calcium-rich systems commonly form C–(A)–S–H-type gels, whereas low-calcium aluminosilicate systems may form sodium or potassium aluminosilicate hydrate, often represented as N–A–S–H or K–A–S–H. Hybrid systems contain overlapping gels. 7.2 GeopolymersThe term geopolymer is often used for binders formed from reactive aluminosilicate sources under alkaline conditions, particularly systems producing three-dimensional aluminosilicate networks. Terminology is not completely uniform: some authors use geopolymer as a subset of alkali-activated binders, while others use the terms interchangeably. Technical specifications should therefore define precursor, activator, composition, curing and performance rather than rely on the label. Advantages may include low clinker content, high early strength under suitable curing, chemical resistance and use of industrial by-products. Challenges include activator cost and handling, variable precursor chemistry, efflorescence, drying shrinkage, carbonation, long-term data and limited standardisation. Sodium silicate solutions can have substantial embodied energy, so life-cycle assessment must include activator manufacture rather than count only avoided clinker. 7.3 Performance assessmentAssessment should include setting, workability retention, heat, strength development, shrinkage, permeability, carbonation, sulfate and chloride exposure, fire performance, reinforcement compatibility and leaching where relevant. Mixes that perform well in laboratory heat curing may not be suitable for ordinary site curing. Robustness to variation is a central engineering criterion. 8. Low-Carbon Cement StrategiesThe principal strategies are: 1. reducing clinker factor through suitable SCMs and fillers; 2. improving kiln energy efficiency and using lower-carbon fuels; 3. electrifying or decarbonising process heat where feasible; 4. capturing and storing or utilising process CO₂; 5. developing alternative clinker chemistries such as calcium sulfoaluminate or belite-rich systems; and 6. reducing concrete binder demand through optimized structural design, packing and quality control. Calcium sulfoaluminate cements can offer rapid strength and lower limestone calcination emissions, but raw material availability, durability evidence and sulfate-related dimensional stability require attention. Belite-rich cements may reduce heat and clinker emissions but generally develop strength more slowly. Limestone–calcined clay cement systems are promising because they combine clinker reduction with reactive alumina and widely available materials. Carbon intensity should be evaluated using a defined functional unit, system boundary and service-life assumption. A binder with lower cradle-to-gate emissions may not be preferable if it causes poor durability, excessive repair or high construction waste. Environmental product declarations and life-cycle assessment should be interpreted critically, especially where allocation of industrial by-product impacts differs between studies. 9. Applied Case: Low-Heat Binder for a Thick Foundation RaftBackgroundThe following is an illustrative engineering case. A 1.8 m thick foundation raft for a large industrial building is to be cast in summer. The structural design requires high later-age strength, low permeability and controlled thermal cracking. Ordinary Portland cement alone produces high early heat. Problem analysisThe risk arises from the combination of large section size, internal restraint, high ambient temperature and slow heat dissipation. A high early-strength cement would shorten construction time but increase peak temperature and thermal gradients. A low-binder mixture could reduce heat but might compromise finishing, strength or durability. ApproachThe project team develops three trial binders: - a Portland cement reference;
- a Portland–slag blend; and
- a Portland–calcined-clay blend.
Each is tested for slump retention, setting, adiabatic heat, compressive strength at 2, 7, 28 and 90 days, chloride migration, shrinkage and thermal properties. A polycarboxylate superplasticiser is adjusted for each binder rather than held at one dosage. The slag blend is selected after demonstrating adequate 7-day strength and substantially lower early heat. The mixture also uses cooled aggregate, night placement, insulated formwork and embedded temperature sensors. For preliminary screening, suppose the measured heat release per unit volume is Q = 180 MJ/m³, concrete density is 2400 kg/m³ and specific heat is 0.88 kJ/(kg·K). Under the adiabatic approximation: ΔT = Q/(ρc) = 180,000 kJ/m³ ÷ [2400 kg/m³ × 0.88 kJ/(kg·K)] = 85.2 °C. This is a theoretical upper-bound-style estimate because real concrete loses heat and hydration is not instantaneously complete. It nevertheless demonstrates that thermal analysis is essential. A finite-element heat and stress model, calibrated using calorimetry and field temperature data, is then used to determine placement size, insulation and allowable temperature limits. OutcomeThe selected blended binder reduces the rate of heat evolution and maintains the required later-age performance. Monitoring shows that the internal–surface temperature difference remains below the project control limit, and no significant thermal cracking is recorded. The result depends on the integrated system: binder chemistry, mixture proportioning, placement sequence, curing and monitoring. Learning pointsThe case illustrates that low-carbon and low-heat design can be aligned, but replacement percentages should not be selected without testing. It also demonstrates why calorimetry, thermal modelling and field instrumentation are complementary rather than alternative tools. 10. Limitations, Governance and Best PracticeBinder performance is sensitive to material variability. SCM composition may change between sources or batches; admixtures may interact unpredictably with sulfate or organic carbon; and alternative binders may lack long-term field records. Engineers should specify measurable performance requirements, establish acceptance criteria and retain traceability of raw materials and trial results. Relevant standards govern cement composition, conformity, testing, admixture use and concrete production. The applicable national and project standards must be identified before specification. Safety controls are essential for caustic activator solutions, fine powders and kiln-derived materials. Environmental claims should be transparent and based on declared boundaries and verified data. AI and digital tools can assist with calorimetry interpretation, mixture optimisation, surrogate modelling and prediction of strength or durability. However, models trained on narrow datasets may fail for unfamiliar SCMs or curing regimes. AI outputs should be treated as decision support, with experimental validation, uncertainty reporting and human engineering accountability. Best practice is to: - characterise cement and SCM chemistry, fineness and variability;
- use calorimetry and trial mixtures when heat or setting is critical;
- specify performance rather than assuming a nominal replacement is universally suitable;
- control curing, particularly for slow-reacting or low-clinker binders;
- evaluate durability under the intended exposure;
- include activator impacts in life-cycle assessment; and
- document compatibility, safety, conformity and change-control procedures.
Chapter SummaryCement performance originates in the interaction between manufacture, clinker mineralogy, hydration and evolving pore structure. C₃S mainly supports early strength and heat, while C₂S contributes more slowly. C₃A and sulfate control setting and aluminate hydration. C–S–H is the principal binding product, whereas pore connectivity, not merely total porosity, strongly controls transport and durability. Hydration heat is a major design issue in massive concrete and must be assessed using calorimetry, thermal analysis and field monitoring. SCMs such as fly ash, slag, silica fume and calcined clay can reduce clinker content and refine pore structure, but their effects depend on chemistry, curing and dosage. Chemical admixtures improve workability and control setting, yet compatibility must be demonstrated. Alkali-activated binders and geopolymers expand the range of available binder systems. They can reduce clinker use but present challenges involving activator impacts, variability, curing, durability evidence and standardisation. Low-carbon cement selection should therefore be based on whole-life performance, safety, conformity and service-life requirements rather than embodied carbon alone. Key TermsClinker: Kiln-produced nodular material that is ground to make cement. C₃S: Tricalcium silicate, a relatively rapid-hydrating clinker phase. C₂S: Dicalcium silicate, a slower-hydrating clinker phase. C₃A: Tricalcium aluminate, a highly reactive aluminate phase. C–S–H: Calcium–silicate–hydrate, the principal binding product of Portland cement hydration. Portlandite: Calcium hydroxide formed during silicate hydration. AFt: Aluminate–ferrite–trisulfate phases, including ettringite. AFm: Aluminate–ferrite–monosulfate and related layered phases. Capillary pore: Pore formed from unfilled original water space in cement paste. Gel pore: Fine pore associated with C–S–H structure. Degree of hydration: Fraction of cement that has reacted with water. Supplementary cementitious material: Mineral material contributing hydraulic, pozzolanic or filler action. Pozzolanic reaction: Reaction of reactive silica or alumina with calcium hydroxide to form cementitious products. Superplasticiser: High-range water-reducing chemical admixture. Alkali-activated binder: Binder formed by reacting a precursor with an alkaline activator. Geopolymer: Generally, an alkali-activated aluminosilicate binder with a polymerised network. Clinker factor: Proportion of clinker in a cement or blended binder. Calorimetry: Measurement of heat flow or heat released during hydration. Thermal cracking: Cracking caused when restrained thermal contraction generates tensile stress exceeding tensile capacity. Carbonation: Reaction of cement hydrates with atmospheric carbon dioxide, commonly lowering pore-solution alkalinity. Review QuestionsShort Answer Questions1. What are the principal functions of gypsum in Portland cement? 2. Distinguish between C₃S and C₂S in terms of hydration and strength development. 3. Why is connected capillary porosity more significant than total porosity for permeability? 4. State two advantages and two limitations of silica fume. 5. What is the purpose of adiabatic calorimetry in concrete technology? Long Answer Questions1. Explain Portland cement manufacture from raw material preparation to finish grinding, including the environmental significance of calcination. 2. Describe the hydration reactions of silicate and aluminate phases and relate the products to strength and setting. 3. Critically compare fly ash, slag, silica fume and calcined clay as supplementary cementitious materials. 4. Explain the principles, opportunities and limitations of alkali-activated binders and geopolymers. 5. Discuss a whole-life framework for selecting a low-carbon binder for reinforced concrete. Analytical / Application Questions1. A massive raft foundation is proposed using a high-C₃S cement in hot weather. Analyse the likely thermal and durability risks and recommend a testing and control programme. 2. A low-calcium fly-ash geopolymer achieves high 28-day strength under heat curing but performs poorly under ambient curing. Explain possible causes and assess whether it is suitable for ordinary site construction. 3. Two binders have equal 28-day compressive strength, but one has higher carbonation depth and the other has higher early heat. Recommend the additional data and decision criteria needed for selecting one for a reinforced-concrete structure. Multiple Choice Questions with AnswersQuestion 1Which clinker phase is most strongly associated with early strength and relatively high early heat evolution? A. C2S B. C3S C. C4AF D. Gypsum Correct Answer: B. C3S Question 2What is the principal binding product formed during Portland cement silicate hydration? A. Portlandite B. Ettringite C. Calcium–silicate–hydrate D. Calcium carbonate Correct Answer: C. Calcium–silicate–hydrate Question 3Why is gypsum interground with Portland clinker? A. To increase aggregate strength B. To regulate aluminate reaction and prevent flash set C. To eliminate all capillary pores D. To replace the need for curing Correct Answer: B. To regulate aluminate reaction and prevent flash set Question 4Which material is generally classified as a highly reactive pozzolanic and filler material? A. Silica fume B. Coarse limestone aggregate C. Entrapped air D. Portlandite Correct Answer: A. Silica fume Question 5For the simplified estimate ΔT = Q/(ρc), what does Q represent? A. Concrete density B. Specific heat capacity C. Heat released per unit volume D. Degree of hydration only Correct Answer: C. Heat released per unit volume Question 6Which pore characteristic most directly controls fluid transport through hardened paste? A. Colour of the paste B. Connectivity of capillary pores C. Clinker particle shape alone D. Nominal aggregate size alone Correct Answer: B. Connectivity of capillary pores Question 7A major potential benefit of ground granulated blast-furnace slag is: A. Guaranteed instantaneous setting B. Increased chloride permeability C. Reduced heat evolution and refined pore structure D. Elimination of all carbonation Correct Answer: C. Reduced heat evolution and refined pore structure Question 8What is a principal technical challenge of many alkali-activated binders? A. They contain no chemically active phases B. Variability of precursors and limited standardisation C. They cannot develop compressive strength D. They require no curing control Correct Answer: B. Variability of precursors and limited standardisation Question 9If Q = 88,000 kJ/m³, ρ = 2200 kg/m³ and c = 0.80 kJ/(kg·K), the adiabatic temperature rise is approximately: A. 25 °C B. 40 °C C. 50 °C D. 80 °C Correct Answer: C. 50 °C Question 10Why must activator manufacture be included in a life-cycle assessment of geopolymer concrete? A. Activators have no environmental impact B. Activator production can contribute substantially to embodied emissions C. Only aggregate production affects emissions D. Life-cycle assessment applies only to Portland cement Correct Answer: B. Activator production can contribute substantially to embodied emissions
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