Aug. 26, 2024
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As world leaders convene at the World Economic Forum&#;s annual conference in Davos to discuss global issues including climate change, they will spend the day surrounded by concrete. Houses, skyscrapers, roads, freeways, bridges, sidewalks, water systems, dams, and more rely on concrete for its unrivaled strength properties, durability, versatility, and low cost. It&#;s no surprise that global demand for cement, which hardens into concrete when mixed with water and minerals, is expected to increase 48 percent from 4.2 billion to 6.2 billion tons by .
In China&#;s recent massive urbanization, the nation used more concrete between and than the United States did in the entire 20th century. While China&#;s use of concrete slows down, consumption in India, Africa, and other developing countries will skyrocket amid economic development, with uses split between residential, commercial, and infrastructure. While essential to building the structures that improve our everyday life, concrete is responsible for 8 percent of global carbon emissions; and 90 percent of these emissions come from the production of clinker, the primary strength-contributing ingredient of concrete.
In accordance with the Paris Climate Agreement, the global concrete industry must reduce emissions by 16 percent by and 100 percent by to stay within the 1.5°C warming carbon budget. This effort will require significant changes across the concrete value chain, but the easiest and most cost-effective measure is to use less material while meeting project requirements. Reducing the demand for carbon-intensive clinker will help put the concrete industry back on track to reaching its climate goals.
The first step toward mitigating the sector&#;s carbon footprint is to use less concrete in each application, even as applications grow. There are several existing and developing methods of ensuring concrete material efficiency that can lead to large carbon savings without changing the material itself. Traditional designs of buildings and other projects aim to minimize cost rather than carbon emissions and layer on excessive design margins. However, recent and ongoing progress in automated design tools allow structural engineers and architects to swiftly explore more structural options for a given project, taking material efficiency into greater consideration.
RMI&#;s publication Profitably Decarbonizing Heavy Transport and Industrial Heat dives into the concrete and steel savings that can be achieved profitably through better structural design. For example, such engineering methods saved New York&#;s Freedom Tower and the Shanghai Tower in China 40 percent and 24 percent of concrete use respectively. As automated design software improves, lean design is expected to be cost competitive (in design time) with current methods and become a main driver of demand reduction.
A second lever is not to use new concrete. In some cases, options like reusing concrete elements from old structures can provide CO2 reductions. However, the right answer will vary from region to region and depend on a host of other factors including the type of construction, design requirements, local availability of materials, and more.
At the same time, building codes and market preferences must be adapted to allow the use of low-carbon concrete. As carbon becomes a key consideration of building our infrastructure, we must close the innovation gap between designers&#; needs and existing technology. Tools like the EC3 Tool efficiently compare the embodied carbon of project design options alongside rigorous testing will pave the way for the low&#;carbon structures of the future.
In addition to reducing the total amount of concrete used in buildings, using less cement per unit of concrete is another effective way to reduce the clinker content and carbon intensity of concrete. To reduce binder intensity without increasing risk we should transition toward bulk cement usage such as ready-mix concrete, in which cement wastage is reduced by up to 30 percent, mix specifications and mix creation are more precise, and chemicals called admixtures can be added to improve concrete properties and reduce cement requirements.
In many countries, builders still prefer the use of bagged cement which leads to both waste and overuse. Industrializing a portion of the world&#;s bagged cement market (currently 42 percent) would yield significant cement savings but requires investment into ready&#;mix plants and cement trucks and considerable change in local market dynamics. In regions such as the US and EU cement usage is already largely industrialized, whereas the market share of bagged cement in India is nearly 90%, offering a huge opportunity for carbon savings. Existing plants are already incorporating a wide variety of chemical admixtures such as dispersants that reduce the need for water and consequently the amount of cement needed. Other admixtures include accelerants that strengthen concrete more quickly and air&#;entrenching agents which allow air bubbles to increase volume and displace solid material input for lower strength applications.
Innovation to create new admixtures as well as increase applicability, efficiency, and cost competitiveness of existing solutions will allow for drastically lower clinker and cement content in concrete while maintaining performance in a given application.
Alternatives to traditional portland clinker cement have also been the subject of much research, but cost, material performance, availability of raw materials, and energy inputs have resulted in limited adoption. While this lever has some merit, large-scale deployment of these niche solutions is unlikely in the short term as they remain relatively customized products, seeking niches in a highly commoditized world.
However, using less ordinary Portland cement has gained ground in another way &#; substituting limited amounts of supplementary cementitious materials (SCMs) in cement blends to partially displace clinker. SCMs exhibit similar behavior as clinker when mixed with water and contribute to the strength of the cement blend, but in most cases cannot fully displace clinker. SCMs include industrial waste products such as ground granulated blast furnace slag (GBFS) and fly ash, calcined clays, natural pozzolans, and ground limestone. The current clinker&#;to&#;cement ratio is 0.72, but the Global Cement and Concrete Association (GCCA) targets an 18% reduction in average global clinker content of cement by .
Selecting concrete with high clinker substitution rates can immediately reduce related carbon emissions of a traditional five-story building by 32 percent with less than a 0.5 percent increase in total construction cost. The ancient Roman Pantheon is constructed entirely of natural pozzolan cement while more modern examples include The Spheres in Seattle and the Iconic Tower in Cairo, both of which use Holcim&#;s low-carbon ECOPlanet cement. While many of these SCMs yield performance benefits, increased setting time and reduced early strength can delay project timelines and incur additional cost in some cases.
Improving the accelerating admixtures that improve the setting time and strength is crucial for greater incorporation of the SCMs in blended concrete. Further testing and updating standards are also crucial to improve adoption. It&#;s important to note, however, that the supply of fly ash and GBFS is expected to decline as their sources, coal power and steelmaking plants respectively, are phased out and decarbonized, making exploration and extraction of other SCMs even more critical to creating greener concrete. Given the global availability of limestone and calcined kaolinite clay, LC3 cement &#; consisting of 50 percent clinker, 30 percent calcined clay, 15 percent limestone, and 5 percent gypsum &#; is seen as one promising approach to the future of low-carbon concrete. As new SCMs and improvements to the performance of current blended cements emerge, the clinker factor and carbon intensity of concrete will continue to decrease. However, time is of the essence in this decisive decade of climate action.
Entities such as First Movers Coalition, ConcreteZero, Industrial Deep Decarbonization Initiative, and others are asking for low-carbon concrete now, and suppliers will need to act to match the increasing demand. Innovation across the concrete value chain can decrease both emissions and costs, pushing the technical limits of carbon intensity and informing policy changes. We need a multi-pronged approach, targeting reductions in concrete, cement, and clinker. The structural engineers of the future will quickly explore an efficient frontier of design options using state-of-the-art software while ready-mix plants deliver less carbon-intensive concrete to projects. These demand reductions are only part of the equation, and supply-side measures such as alternative fuels, electrification, and carbon capture will have to eliminate remaining emissions.
Through the Mission Possible Partnership, RMI has partnered with Energy Transitions Commission, Systemiq, World Economic Forum, European Cement Research Academy (ECRA), and GCCA to explore each of these decarbonization levers in addition to decarbonization levers on the supply side in the soon-to-be-released Cement Sector Transition Strategy. The concrete and cement industry is at the cusp of a radical transformation in its journey to the net-zero energy transition.
Currently, the production of one ton of ordinary Portland cement (OPC) releases considerable amounts of CO2 into the atmosphere. As the need and demand for this material grows exponentially, it has become a challenge to increase its production at a time when climate-related problems represent a major global concern. The two main CO2 contributors in this process are fossil fuel combustion to heat the rotary kiln and the chemical reaction associated with the calcination process, in the production of the clinker, the main component of OPC. The current paper presents a critical review of the existent alternative clinker technologies (ACTs) that are under an investigation trial phase or under restricted use for niche applications and that lead to reduced emissions of CO2. Also, the possibility of transition of clinker production from traditional rotary kilns based on fuel combustion processes to electrification is discussed, since this may lead to the partial or even complete elimination of the CO2 combustion-related emissions, arising from the heating of the clinker kiln.
Keywords:
alternative clinkers, CO2 emissions, OPC, process electrification
The history of cement has had a major impact on the progress of our civilization during the last century [1]. This cheap mineral binder, when in contact with water, goes through a set of relatively complex physicochemical reactions, that result in a stone-like hard material. This allows the production of mortars, cement mixed with water and sand, and concrete, cement mixed with water, sand and aggregates such as gravel and slag [2]. Concrete is, not only extremely resilient and durable but can also bear heavy compressive loads and resist severe environmental conditions. These set of properties combined allowed concrete to position as the man-made most widely used material in the world [3]. Due to the high demand for concrete, 4.3 Gigatons of cement were estimated to be produced globally during the year [4].
However, the amount of CO2 released during the production of OPC has a very strong environmental impact. In fact, the production of one ton of clinker releases about 0.83 tons of CO2 and the production of one ton of OPC releases about 0.54 ton of CO2 [5] making this industry responsible for 5% to 8% of total anthropogenic greenhouse gases [6] The two main sources of CO2 emissions resulting from cement production are: (i) the decarbonation of limestone since CaCO3 is decomposed into CaO and CO2 at temperatures above 550 °C, with this contribution representing about 60 to 65% of the total CO2 emissions [7] and (ii) the fossil fuel combustion to heat the cement kiln, which is responsible for the remaining 35 to 40% of the emissions.
Hence, within the scope of the United Nations (UN) agenda [8] and also driven by the increasingly higher CO2 emission taxes it has become a target and a challenge for the cement industry to develop new binders with a lower ecologic footprint, that can be produced at a large scale, so that it can be used as a commodity, without compromising the technical, economic and workability qualities characteristic of OPC. As it became clear from the 26th UN Climate Change Conference of the Parties (COP26), held in Glasgow in November , managing the pressure for the unavoidable need of social development together with the agendas of environmental sustainability and climate change control will be the challenge of the century, and the cement industry itself is a relevant key player in this fundamental discussion.
Until now, the methods that have been studied to mitigate CO2 emissions in cement production follow five main approaches [9]:
Reduction of the cement-to-clinker ratio, by replacing clinker with supplementary cementitious materials (SCM&#;s);
The use of alternative fuels in the production of clinker together with the increase of energy efficiency of the kiln process;
Development of alternative clinker technologies (ACTs), that lead to lower CO2 emissions.
Carbon capture, use and storage (CCUS), i.e., the sequestration and use of the emitted CO2 for specific applications;
Electrification of the clinker production process, especially if renewable electricity produced from non-fossil energy sources is used;
CCUS technologies consist of the capture, transport, use and storage of CO2 [10]. More interestingly, a number of research projects have also explored the CCS possibility, bringing insights into the use of CO2 for other applications, namely the production of hydrocarbons or alcohols, through the reaction of CO2 with H2 [11]. Yet, in general, CCUS technologies are still costly and in a demonstration stage of Technology Readiness Level (TRL) [12]. On the other hand, the cement kiln main stack flue gases have high amounts of impurities such as N2, SOx, NOx and CO [13], which make difficult the capture and direct use of pure CO2. Further research and development will therefore be needed to reduce the cost of the capture step and to increase the TRL of CCUS technologies to render them an economically viable solution to be applied in the cement industry. The work of Plaza et al. [10] provides a comprehensive and interesting overview of the CCUS technologies that have been evaluated in the cement industry at the pilot scale and also the plans for further industrial implementation.
Regarding SCMs, it is worth mentioning the main conclusions of the working group initiated by the United Nations Environment Program-Sustainable Building and Climate Initiative (UNEP-SBCI) published in [14]. The group concluded that Portland-based cement approaches will dominate in the near future due to economies of scale, levels of process optimization, availability of raw materials and market confidence, but that two product-based approaches can deliver substantial additional reductions in their global CO2 emissions, over the next 20&#;30 years: increasing the use of low-CO2 additives, or supplementary cementitious materials (SCMs), as partial replacements for Portland cement clinker and more efficient use of OPC clinker. Several types of SCMs may be added to cement during concrete production, including: rice husk ash, silica fume, fly ash and ground granulated blast furnace slag (GGBFS) [15]. For rice husk, the recommended replacement level is 30%, this SCM densifies the concrete matrix and reduces the volume of voids [16]. For silica fume, previous results showed that a replacement of 5% produces the best performance, with an increase of workability, strength and durability of the material [17]. Fly ash may replace up to 70% of the cement, allowing the production of so-called high-volume fly ash concrete (HVFA) [18]. Finally, GGBFS can replace up to 40% of cement without the need for a superplasticizer [19]. However, a major disadvantage of SCMs, pointed out by the (UNEP-SBCI) [14] working group, is that high blended cements may exhibit slow early-age strength development and uncertainty on the long-term durability [20]. Also, the concrete produced with OPC+SCM may present lower flowability [12], hampering the pumping, spreading, molding and compaction of the material [20]
The mix of fossil fuels commonly used to heat the cement kiln (e.g., petcoke, coal, natural gas, fuel oil, mazut, etc.) are already being replaced, to some extent, with alternative fuel such as waste tires, sewage sludge, animal meal, waste oil, waste paper, plastics, textiles, agriculture and biomass wastes, amongst other. Nevertheless, these alternative fuel solutions only represent up to 10% of the reduction of the total CO2 emissions in cement production [21]. According to CEMBUREAU&#;s Roadmap to Carbon Neutrality in , altogether, the replacement of fossil fuels by non-recyclable and biomass waste, and the use of alternative raw materials, will deliver 15% of the CO2 emissions reduction in the cement industry in [22].
A much more interesting approach in what concerns energy supply is the electrification of the process, especially if the electricity comes from low-carbon or non-fossil sources [23]. We will come to the topic of electrification at the end of this paper due to the key importance that it may represent in the near future, particularly having in consideration the European Green Deal agenda and the ongoing green agendas in the rest of the world. Nevertheless, we must have taken into consideration two fundamental aspects regarding the electrification of the cement industry:
The best available technology (BAT) of OPC production cannot be easily converted into a fully electrified process, since it would require very significant changes not only in the technology itself but also in the dimensioning of the industrial installation due to the lower volume of material (gases and dust) in circulation.
At least 60% of the released CO2 comes from the decarbonation stage, while only 35 to 40% of the remaining CO2 emissions come from the energy needed to promote the high-temperature reactions that characterize the clinkering stage. Thus, acting in the material composition stage is mandatory to achieve a significant reduction of CO2 emissions in cement production. Therefore, at the present point, other emerging technologies or alternative materials will also play an important role in emissions mitigation in the medium/longer term.
This paper intends to provide a critical review on this last topic: the use of alternative binders, focusing on the threats and opportunities that can be open in a long-term vision, at a moment in which the cost of CO2/ton almost reaches the production cost of one ton of clinker.
Concerning ACTs, these approaches have to be able to generate, not only a similar economic value to that of OPC, accomplishing the necessary reduction of CO2 emissions, but at least, present a similar competitive performance. Some of the most critical properties, which must be taken into consideration are:
Mechanical performance, both at early ages and later ages;
Rheological performance, enabling an adequate pumping, spreading, molding and compaction of the material [ 20 ];
Reduced chemical shrinkage, since this phenomenon causes serious loss on the durability and bearing capacity of concrete structure, increasing the risk for cracking and decreasing the lifespan of the structures [ 24 ],
Chemical stability, which will be translated into structure durability when submitted to the natural elements.
The fulfillment of the before mentioned requirements is the basis for the development of new alternative clinker technologies, however, any emerging technological solution should be able to compensate for the substitution of the existing OPC production BAT in terms of replacement investment. This is clearly a difficult path. However, it is also clear that the actual level of CO2 emissions related to OPC production is not compatible with the neutrality goals set by the authorities for the cement sector. Therefore, the development of new types of binders as alternatives to OPC may play a role of paramount importance in the quest for cement sector carbon neutrality. Before deepening into some of the new binders commonly presented as alternatives to OPC, we should revisit the CaO-SiO2 system, which is the chemical base of OPC and the reason for its own success during the last century.
To frame the question of CO2 emissions in the production of hydraulic binders, it is important to shortly revisit the binary CaO-SiO2 system [25] ( ), which is the chemical base of OPC and, to some extent, the ACTs that we will discuss further on.
Open in a separate windowThere are two important characteristics of this system that impact the CO2 emissions related to the production of hydraulic binders, such as OPC.
The first one is that CaO does not abundantly exist in the earth&#;s crust and must be synthesized from limestone (CaCO3), according to the reaction:
CaCO3&#;CaO+CO2
(1)
Reaction (1), the decarbonation of limestone, is the cause behind the largest source of CO2 emissions in cement production. Thus, reducing the amount of CaO in the binder results directly in a reduction of CO2 emissions.
The second one is the hydraulic ability, or reactivity, of the phases that are present in the CaO-SiO2 system. Besides the main oxides, CaO and SiO2, in their different allotropic forms, there are four monophasic domains in this system: alite or (CaO)3SiO2, belite or (CaO)2SiO2, with five allotropic forms: α, α&#;H,α&#;L, β and γ, rankinite or (CaO)3(SiO2)2 and wollastonite or CaO·SiO2, which has two allotropic forms, α and β (from now on, we will use the common nomenclature used in cement literature; C3S for alite, C2S for belite, C3S2 for rankinite and CS for wollastonite. We will also use A, for Al2O3, F, for Fe2O3, Ŝ, for SO3 and finally H, for H2O).
OPC clinkers are formed essentially by alite, with smaller proportions of belite. However, from the binary diagram above, it is evident that producing clinkers in the rankinite or wollastonite domains would result in a decrease in CO2 emissions. It happens that only alite and belite are hydraulically active [26], with alite presenting higher reaction kinetics when compared to belite. That is, as the amount of SiO2 increases, the hydraulic reactivity of the calcium-silicate phases decreases. The reason for that is the fact that there are significant modifications in the structure of the calcium-silicate crystalline phases as the C/S ratio decreases, from 3 (alite) to 1 (wollastonite). These changes are essentially related to the organization of the SiOx units in the crystals, as well as to the spatial distribution of the Ca atoms in the crystal network [27]. Whereas in alite and belite polymorphs, the [SiO4]4&#; groups are isolated and present some degree of disorder in the superstructure, in rankinite, the Si and O atoms are arranged in sorosilicate groups [Si2O7]6&#;, in which a central O connects with two SiO3 units, whilst in wollastonite polymorphs, Si and O atoms are arranged in long parallel dreierkette-type chains of {[SiO3]2&#;}n units and there is an increase in the number of the bridging oxygen atoms in comparison to rankinite [27]. This structural shift among the four types of calcium silicate crystals (alite, belite, rankinite and wollastonite) can be summarized using the Qn terminology, that designates how a given silica tetrahedron is connected to another silica tetrahedron in a given crystal, as shown in : Q0 (black), Q1 (green), Q2 (orange), Q3 (blue) and Q4 (yellow), depending on how many O-Si species are connected to the central silicon atom. While in the hydraulically active phases, alite and belite, the coordination is Q0, in the non-hydraulically active phases, rankinite and wollastonite the coordination is Q1 and Q2, respectively. Experimental NMR results indicated that the Q0 units dissolve preferentially during the hydraulic reactions, resulting in C-S-H structures, predominantly formed Q1 and Q2 units [28].
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Further reading:Alite constitutes 50&#;70% of OPC and, upon hydration, is responsible for the strength development up to 28 days [29]. Belite may constitute 15&#;30% OPC and its contribution to the compressive strength can only be seen at later ages [29]. Both alite and belite, when hydrated, form a non-stoichiometric calcium silicate hydrate phase (C-S-H) and, as a secondary product, calcium hydroxide Ca(OH)2 or portlandite.
The C-S-H typically obtained from the hydration of alite or belite presents a C/S ratio of approximately 1.7 [30], with the excess of calcium, inevitably producing around 15&#;20% wt of portlandite [31]. However, the C/S ratio theoretically depends on the concentration of Si and Ca ions that are in the solution and can change from 0.8 to 2.1 [32]. Furthermore, through computational calculations, Pellenq et al. [33], reported that a binder with a C/S ratio between 1 and 1.1 would present crystalline domains characterized by improved mechanical performance.
The hydraulic reaction of OPC is an exothermic process that releases approximately 250 J/g of cement during the first 72 h of hydration [34]. This reaction starts with an induction period, characterized by an initial dissolution of species that are released into the aqueous solution. The species continue to dissolve until their concentration reaches a saturation condition, further leading to the nucleation and growth of the hydrated phases. At this point, there is an accelerating period in which occurs an extensive heat release, corresponding to the massive precipitation and growth of C-S-H and portlandite phases [35]. The precipitation and growth of these phases will result in the setting of the binder and in the increase of its mechanical strength with time. This is the basis of the alite/belite-based binders, the group to which OPC belongs.
The next section will briefly describe the binders that, although in different stages of development, have the potential to become alternatives to OPC in a perspective of CO2 emissions reduction.
The seek for carbon neutrality in the cement industry in the medium to long term will certainly depend on the possibility of scaling-up alternative clinker technologies (ACTs) encompassing new binder formulations and also new technological processing routes. The reason for that is the fact that hydraulic binders are a commodity whose demand will increase for sure in the next decades, namely with the economic development of large population countries in Asia, South-America and Africa [36]. Therefore, the cement industry cannot depend only on the availability of SCMs for large mass production of hydraulic binders or on the development of affordable CCS, it should pursue also the possibility of developing hydraulic binders with near to zero CO2 emissions. This long-term goal in the cement industry can only be obtained by reducing substantially the calcium content of the binder and by combining it with processing technologies that enable the full electrification of the processes. How far are we from this goal? In the next points, we will revisit the state-of-the-art in view of the possible answers to this question, having in mind that the main requirements for ACTs that can replace OPC as a widespread commodity material are:
The capacity to mimic OPC properties, namely the production of mortar, concrete and reinforced concrete.
A reduction of CO2 emissions large enough to justify the substitution of the BAT for cement production, since this represents a widespread technology with thousands of dedicated plants all over the world.
A small impact on the need for modifications of national and international standards for cement use.
According to some authors [14], it will be difficult to turn around these requirements in order to develop a binder completely different from OPC in a short-term period, adapting it to environmental needs. In fact, to be able to achieve a significant breakthrough in this area, a large investment in research and large-scale demonstration projects is necessary. In addition, it will also be necessary to educate and train the consumers for the acceptance of these novel binders in the construction market [12]. However, even after facing all these difficulties for a long period of time, the hope of producing cement with near-zero CO2 emissions still remains, with a considerable number of ACTs continuously emerging. Thus, the investigation on this topic has significantly increased in the last two decades and, as a result, a number of alternative binding materials, different from OPC not only in formulation but also in their production routes and even application, have emerged and have been reported in the literature.
At the time this paper is written, it is difficult to say which of these ACTs, if any or all of them, can become an alternative to OPC in the near future, but certainly, the need for substantial CO2 reduction in cement production, together with the increasing demand for cement in the world, will bring this forward as a key question. The next paragraphs will be dedicated to a review of the alternative binder technologies that presently exist, with some of them being reported in the scientific literature as possible alternatives to common OPC [37]. This paper will be focused only on ACTs, without considering activated slags and geopolymers, since we believe that this is a sufficiently broad field to justify a focused review (e.g., for a recent deep review on this topic, see Provis et al. [38]).
Belitic binders are not a recent discovery. In fact, they have been used since the times of the Roman Empire [39].This type of clinkers has essentially belite in its constitution and, therefore, its reaction process requires 10% less limestone, as it results from the analysis of . Also, the synthesis of belitic clinkers requires lower processing temperatures, compared with the alitic-based clinkers, which also translates into a reduction of the CO2 emissions resulting from the furnace heating [39]. In addition, its lower heat of hydration [40], its better rheological properties and its improved durability at later ages, due not only to the smaller proportion of CH that is formed in the hydration but also because of its densely packed structure are advantages of belitic clinkers when compared to alitic ones.
Nevertheless, belite clinkers present a low early-age strength, due to their slower hydraulic kinetics. In fact, Kotsay et al. [39], reported, that after 28 days, the degree of hydration of the belite can be four times lower compared to the alite phase and, only after one year of hardening the strength of alite and belite hydrates are comparable. There are two main reasons for the lower hydraulic reactivity of belite at early ages: one is that the H2O molecules have more difficulty in penetrating the belite lattice, due to its densely packed structure [39], the other is that the Ca2+ ions attached to the SiO4 tetrahedron are less easily dissolved [41]. Therefore, the first step of the hydraulic reaction, the dissolution step, is slower in belite, as compared with alite. It has been disclosed that the incorporation of metal oxides into the lattice of belite, as substitutes of Si, increases the hydraulic reactivity at early ages of belite-rich clinker due to a higher infiltration of H2O molecules into the lattice, accelerating the dissolution of the material [42].
A completely different approach to belitic clinkers was proposed some years ago in which hydraulic binders with C/S = 1.4 were produced by inducing the formation of a dendritic belite phase embedded in an amorphous calcium-silicate phase [43]. These hydraulic binders were produced by a process involving heating the raw materials with a specified C/S ratio to a temperature below the liquid&#;s surface, followed by a two-step cooling ramp, in order to obtain during solidification a dendritic morphology of the crystalline phase. After milling the clinker obtained by this process, and by adding up to 25% of water, the paste set, showing mechanical performance that went up to four times higher than the values obtained for a reference round shape belite clinker, opening the possibility of developing a novel belite-based clinker with increased reactivity.
Therefore, belitic-rich clinkers can be used in conditions when factors such as low heat release and high later age strength are important parameters, for example in high-performance concrete, or large volume structures [40]. Nevertheless, although the substitution of alite by belite may reduce CO2 process-related emissions by up to 10%, it is still far from the goals defined for the cement industry in the global agenda for climate change.
Calcium sulfoaluminate cements (CSACs) are a belitic type of cement, which were developed in the s [44] with the intention of compensating for the lower early-age strengths typically observed in belite-rich cements [44]. Typical raw materials used in the production of CSACs are limestone, calcium sulfate and aluminum-rich minerals or industrial by-products. Its production is carried out at temperatures around °C, approximately 200 °C lower than the necessary to produce OPC clinker [44], and is generally easier to grind [45].
The main clinker phases in CSACs are ye&#;elimite, Ca4(AlO2)6SO4, belite and calcium sulfate CaSO4 [44]. Since ye&#;elimite rapidly hydrates, it compensates for the loss in early-age strength in belitic clinkers [46]. As ye&#;elimite dissolves it enables the reaction with calcium sulfate and water and allows the formation of ettringite (Ca6Al2(SO4)3(OH)12·26H2O) and microcrystalline aluminum hydroxide Al(OH)2 [45]. Ye&#;elimite contains about 50% wt. of Al2O3 thus, the required alumina content in the raw materials to produce CSACs is above 20%, which can come from sources such as bauxite or industrial by-products, such as the ones proposed in the work by Canbek et al., namely red mud and sulfate-rich/high-lime fly ash [46]. However, the availability of low-cost sources of alumina-rich raw materials is certainly a limitation for the generalized use of CSACs [46].
Cement with high ye&#;elimite contents (>50% wt) can be used in combination with OPC to produce a fast-setting, rapid hardening cement [45]. CSACs cements with less ye&#;elimite (25&#;50% wt) contain significant amounts of belite (30&#;50% wt) and ferrite (5&#;20% wt) and can be a sustainable replacement material for OPC [45]. When compared to OPC, in some areas, the use of CSACs has been shown to have better performance when applied to concrete. They present lower shrinkage, lower cracking and higher resistance to freeze-thaw damage [45].
Another alternative to the CSACs is belite-ye&#;elimite-ferrite cement (BYFC), which presents a lower cost than CSACs, achieved by reducing the use of the most expensive aluminum-rich raw materials, resulting in a higher proportion of silicate and ferrite phases [47]. The ferrite phase, 4CaO·Al2O3·Fe2O3 has a slower hydration process than Ca4(AlO2)6SO4, therefore, ye&#;elimite, anhydrite and gypsum are the first phases to react, followed by ferrite and belite [48] Since the hydration of ye&#;elimite is faster than that observed for belite, the increase of compressive strength is similar to OPC [49].
Both CSACs and BYFCs can be produced in common clinker plants, essentially by changing the raw materials that are used to feed the kiln [47].This is a major advantage in terms of investment cost since it would allow the production of both types of material within the same facilities without the need for substantial process modifications. However, both CSACs and BYFCs present susceptibility to the carbonation process, caused by the dissolution of the atmospheric CO2 into the pore paste. This reacts with the hydrated products causing an increasing CO32&#; ion concentration. The formation of this anion has severe consequences facilitating the deterioration of ettringite [45], and raising the acidity of the system leading to the corrosion of steel rebar, used to reinforce concrete [44].
Solidia Cement patented in [50], is a non-hydraulic binder produced using the same raw materials as OPC, but with a lower amount of CaCO3 and a kiln temperature around °C, which allows a reduction of the CO2 emissions by 30% [50,51]. This binder has an overall C/S molar ratio of ~1 and it is formed essentially by wollastonite/pseudowollastonite, with smaller amounts of rankinite (13% wt), and belite (~3% wt) [52]. This mixture of calcium silicate phases has the ability to harden by a carbonation process and, consequently, there is no need for water consumption for the reaction to occur [51].
This cement is produced by feeding the granulated raw material into a natural gas-fired rotary kiln. The calcium silicate compositions created in the rotary kiln emerge in a &#;clinker&#; form, that is, in small granules with diameters of approximately 1 to 4 mm. The clinker is then ground to a powder with a mean particle size of approximately 12 μm. To produce concrete, this material is mixed with aggregates, sand and water. The cure of the concrete takes place when the mixture is exposed to a high-concentration gaseous CO2 environment (60&#;90%) [53] which allows the reaction of the binder phases and the production of CaCO3 and SiO2.
One of the most interesting characteristics of this binder is precisely the fact that the curing process can capture up to 300 kg of CO2, per ton of binder [51] and is only limited by the ability of gaseous CO2 to diffuse throughout the particles [51]. To speed up the curing process heat may be applied, these temperatures, if needed, can even be higher than 60 °C since there is no formation of ettringite [53]. The CaCO3 that is formed fills the pore space within the concrete, creating a dense microstructure and, the SiO2 is formed at the outer surface of the reacting cement particle [51].
Although Solidia Cement does not hydrate, water plays an important role in its forming and curing mechanism. Water contributes to the good flowability of the material and also acts as a permeating agent contributing to the cure development that occurs through a counter diffusion process where water molecules are replaced by CO2 molecules [53]. However, since the water is not consumed, 90% of it can be recovered, while the remaining is retained in the cured concrete [52]. The mechanical properties of the concrete are equivalent to those of OPC, and they are achieved within a shorter curing period [52]. Another characteristic of this binder is that the carbonation process only releases about 87 kJ/mol of heat during curing which is dissipated through the evaporation process of the water that is used in the concrete preparation [53].
Even though this is a promising cement, its application and use are limited, since its curing process must be conducted under very controlled CO2 concentration conditions, which, so far, can only be provided in a ready-mixed concrete plant [12] impairing to some extent the generalized use of Solidia cement as a substitute of OPC.
Celitement® is a patented hydraulic binder, developed by the Karlsruhe Institute of Technology (KIT) in collaboration with the SCHWENK Zement KG industry [54]. Its concept is to synthesize and stabilize a short-time precursor of C-S-H to produce a hydraulic binder [55]. This material is characterized by its low energy demand during its production process, which enables a reduction in CO2 emissions [55]. The Celitement production relies on the formation of an intermediate phase that is prior to the development of the C-S-H. This intermediate phase has a similar structure to C-S-H, but a slightly different chemical composition and is referred to as hydraulic Calcium Hydro Silicate (hCHS) [56].
The production method of Celitement, uses raw materials CaO, in the simplest case, or Ca(OH)2 and quartz sand [57]. It requires a calcination stage (around °C) that is applied only to the CaCO3-rich raw-material, and hydrothermal processing of the raw mix that takes place in an autoclave at a temperature of 200 °C and at a saturated steam pressure of 12 bar, which facilitates the full electrification of the process. The product that results from the autoclave is stabilized by a strong hydrogen bond which makes it non-hydraulically active [55]. In a second step, this product goes through a special grinding operation [55] that enables the destruction of the hydrogen bonds [57] and, around the cores of the non-reactive co-milled silicates, a new amorphous calcium hydrosilicate (hCHS) is produced [55,56,57]. The final produced material is mainly amorphous, with highly disordered phases and high specific surface, containing in its composition Q0 and Q1 silicate species [57,58]. After 17&#;20 h of hCHS hydration, a well-ordered C-S-H phase is formed, releasing a very low heat of hydration (120&#;150 J/g) and promoting an early-age strength comparable to OPC [55].
The Celitement approach is based on a technology that completely differs from the one known today for the production of Portland cement, leading to what may be a significant drawback in its industrial implementation. Nevertheless, this new technology is already under the demonstration phase, with a recent expansion to the pilot plant, constructed in , allowing the production of approximately 700 kg per day [59].
Another alternative, developed and patented internationally by CIMPOR and Técnico-Lisbon, is an amorphous low-calcium hydraulic binder characterized by a raw mix containing 33% less CaCO3 than the typical OPC, and an overall C/S ratio of 1, allowing for a reduction of more than 25% of the usual OPC clinker process-related CO2 emissions [60,61].
The production process of this binder allows the use of traditional raw materials, such as limestone, clay, marl, sand, etc., and consists in fully melting the raw mixture, at a temperature of °C, followed by a rapid cooling [59]. The resultant product is mostly amorphous (~94% wt), with the presence of a small amount (<10%) of pseudo-wollastonite [60]. It should be pointed out that the full melting of the mixture may facilitate the electrification of the process through plasma or electrical arc melting, which may lead to a scenario where the effluent gas stream is solely fed by the CO2 generated by the calcination of the raw meal. Such a highly CO2 concentrated gas stream could potentially be combined with green H2 to produce methanol and other hydrocarbons [62,63].
The reactivity of this novel binder comes, mostly, from its amorphous phase, yet even though existing in a small amount, the presence of pseudo-wollastonite has been shown to have some influence on the hydrated product performance [64]. Better compressive strength results were obtained when this phase was produced in an amount of ~6% wt [64]. An investigation on the hydration of this binder observed, by 29SiMAS-NMR spectroscopy, that the least coordinated Qn units, Q0 and Q1, play a very important role in the hydration since they appear to be very prone to polymerize and convert into C-S-H structures that are similar to tobermorite [60]. By changing the structure from crystalline to amorphous, the arrangements of Si&#;O bonds become more disordered, which favors their dissolution [60] and, consequently, the further precipitation of equilibrium hydration products [65].
The behavior of this novel amorphous binder was further studied by Santos et al. [28], which investigated the effect of different alkaline activators (Na2CO3 and a mixture of NaOH and Na2SiO3) on the mechanical strength and structural characteristics of hydrated pastes. It was observed that, when activated, those pastes presented increased hydration kinetics, allowing for an improvement in their mechanical performances. Furthermore, the most competitive results were obtained when the pastes were activated with Na2SiO3, with a 3 wt% total content of Na2O, obtaining pastes with strengths comparable with those of traditional OPC [28].
In terms of technological development, this approach presents a main drawback, which is the need for a pyro-processing step that is 100 °C superior to that of OPC and, the requirement of a sodium silicate solution for activation, in order to present competitive early-age strength.
In addition, since the processing conditions require the formation of 100% liquid phase, some adaptations to the usual BAT of clinker production may be required in order to industrially implement this type of technology.
shows a simplified flow chart containing the stages considered for the production of the alternative binders mentioned in the present review, evidencing the differences of the process in the various ACTs approaches. From , it becomes clear that in the present state, research should be pursued in all the presented solutions. From the several technological proposals contained in , it should be noted that only the Celitement® and the X-Clinker approaches presently consider a scenario of full process electrification, while the other approaches essentially follow a fuel combustion-based design, similar to the existing BAT. The proximity to the BAT for clinker production is certainly an advantage for the industrial implementation of some of the alternative binders mentioned above, however, when looking forward through a perspective of cement industry decarbonization, it is the author&#;s belief that full or partial conversion of the existing fuel-based technology to electricity-based technology should occur in the next decades.
Open in a separate windowshows a detailed description of the various sources of CO2 emissions within the production processes considered for the ACTs reviewed, evidencing the separation of the contributions for the thermal and material-related emissions. The CSA, X-Clinker and Celitement approaches lead to material-related CO2 emissions smaller than 0.35 tons per ton of clinker. If full electrification of the process for these ACTs with green electricity is achieved, a target for CO2 emission in cement production smaller than 0.25 tons of CO2 per ton of cement is within reach of the cement industry in the upcoming years.
Open in a separate windowCertainly, the reduction in the ecological footprint in the cement industry encompasses the substitution of fossil fuel in the cement kiln for electrification in the heating process. In fact, as the cost of solar photovoltaics, wind power and battery storage decreases, the coupling of industry electrification with renewable electricity supply has become a potential solution for industrial decarbonization [66]. In particular, the electrification of the cement production has become a more feasible alternative to the current method of combustion, and unlike gas furnaces, electric furnaces have very low direct emissions of CO2, NOx and SOx, however electric furnaces may have shorter lifetime periods than conventional furnaces [67]. According to the work of Madeddu et al. [68], the cement industry has the potential for 36% electrification, which essentially considers the calcination of limestone, whilst the energy necessary for clinker burning is not considered electrifiable at this stage of technology development. However, in the report of the CemZero project [69], it is referred that the production of cement clinker by means of plasma technology appears to be technically possible. This CemZero project is being conducted in Sweden, as a collaboration between Cementa and Vattenfall, and aims to test different technologies for the total or partial electrification of the cement production process.
Their study indicated that the production costs of cement in an electrified process appear to be doubled in comparison to today&#;s technology but could be competitive compared to other technological options for radical emission reductions [70].
Another project that points to an electrically powered calcination process is the LEILAC, which is being developed by a large consortium of companies and foresees to implement a fully operational plant by [71]. This project assesses, through a direct separation perspective, the feasibility of CO2 capture and storage, by means of the generation of a highly CO2 concentrated gas stream from the calcination stage important development is the electrochemical approach that converts CaCO3 in Ca(OH)2 and may represent a real alternative solution to overcome the CO2 emissions from the decarbonation process in cement industry. This technology is able to capture excess power and, through electrolysis, convert limestone into hydrated lime, working similarly to a battery. This process was already tested at the laboratory scale, and they reported that a future implementation on a larger scale could allow for a decentralized, automated, easy to deploy, easy to start-up and shut down cement plant [72]. Processes of combining calcination and CO2 capture by using electricity were also reviewed recently by Tokheim et al. in a conference paper [73]. Due to the critical importance of the topic of electrification in the framework of ACTs a short review of these processes is presented in the following points.
This technology can produce temperatures above °C and is currently used as waste treatment and in some niches in the steel industry [74]. Its implementation in the cement industry may open the possibility of using recycled CO2 as plasma gas [75], which further benefits the goal of CO2-free cement industry. The main disadvantage of using thermal plasma is the overheating of the reaction media [76], which can impair the clinker performance by changing the phases present at room temperature, and also the short lifetime of the electrodes. As referred above, the use of plasma was one of the technologies that CemZero tested on a laboratory scale, being reported that it is possible to produce cement clinker of regular quality by using plasma gas as a heat source. Nevertheless, a larger-scale test must be performed, since one concern with the use of this technology is how to maintain the rate of heat transfer in a rotary kiln [69].
In this approach, a metal surface is heated by running a current through a resistive element, which usually is protected by a shroud. Then, the heat can be transferred either by gas, through high-velocity convection, or directly to the material, through radiation or conduction, if it is possible to promote the direct contact between the raw meal and the resistive heater. This type of technology is already used in glass melting furnaces and can either be applied in combination with another heating method, acting as a boost in gas-fired furnaces [77], or as a complete replacement of the traditional heating method, providing a completely electrified production [78,79]. Typically, electric glass furnaces use a vertical melting process [80]. The furnace is continuously fed at the top side and the melted material leaves the furnace through the bottom. The heating provided by running a high current into molybdenum electrodes [80] whose configuration arrangement influences the homogenization capacity of the mixture [81]. Jebava et al. [81] reported that by distributing the electrode into a longitudinal central row, there is an optimization on the utilization of space and the highest melting performance. These types of furnaces can provide an efficiency of up to 87% and a wide range of high-temperature processes [82].
By using electromagnetic waves, the electromagnetic heating technologies are able to provide high temperatures, with an efficiency of up to 90% [82]. Furthermore, it has the advantage of being able to generate rapid heat within a target material [82]. Some examples of these technologies include:
Induction heating occurs when an electrically conducting object is placed in a varying magnetic field. The friction between molecules when the material is magnetized first in one direction, and then in the other is converted into heat [83]. To cool the induction furnace, water-cooled coils are used. This technology allows almost instantaneous heating or cooling of the calciner. However, there is a risk of overheating the product when the heat necessary for the calcination is inferior to the heat provided by the induction system [84]. This type of technology is able to reach high temperatures fast and is currently applied in induction furnaces used for metal melting [85]. However, it is not currently seen as a potential solution for processing ceramic materials [82].
The heat necessary for calcination can be delivered by microwave through a radiation form, by transferring direct energy in the form of electromagnetic waves into the material. Corrêa et al. [86], investigated the use of a microwave oven in the calcination process reaching a temperature of °C. The team reported that this method provides better results in terms of reaction time, energy consumption and emission of polluting gases when compared with traditional methods. Furthermore, the use of a refractory ceramic coated with copper oxide reduced the energy expenditure and accelerated the process to be twice as fast. Microwave heating is currently used in the conversion of biomass and by-products and also, in waste processing, although mostly at the laboratory scale [87]. Even though this technology is able to provide a rapid internal heating of large volumes, large production scales presents high operation costs, which presently hinder its use in a generalized form [82].
It has to be taken into consideration that the electrification of any industry is highly influenced by energy and environmental policies [74]. Not only, can the electrification cost be challenging, but also the electricity prices must be competitive. Moreover, industry electrification only reduces greenhouse gas emissions if renewable-generation capacity is added to meet its electricity demand. Nevertheless, in the current conditions of climate change, a complete shift from an oil and gas economy to a green energy source has been associated with the future of energy [88]. In fact, the global renewable energy generation capacity has progressively been increasing, and it is estimated that by , more than 80% of electricity will come from renewable sources [89]. Currently, in the EU-27, renewable sources already make 34% of electricity consumption, with the majority coming from wind and hydropower and a small part from solid biofuels and solar power [90]. Hence, as the prices of renewable electricity and electric equipment continue to drop [66,91], the electrification of the cement industry can be an important option to achieve a high reduction of CO2 emissions.
To be able to seek neutrality in the cement industry, the current method of cement production must change. There are many potential routes to lower CO2 emissions, and some are more prone to succeed than others. This paper reviewed and discussed a variety of alternative clinker technologies for the partial or complete substitution of OPC. The performance of these materials is largely dependent on their physical and chemical characteristics, which have a major influence on its curing process and, consequently, on the binder&#;s mechanical performance. In some of the cases, further studies for a complete characterization of materials properties are needed.
Nevertheless, the goal of CO2 neutrality in the cement industry can only be reached through an extended replacement of OPC by green alternative binders, as well as through a transition from fossil fuel technology to a green energy-based technology.
The CO2 process-related emissions, assuming that the main calcium source is limestone, are shown for different ACTs, and very significant differences among these materials can be observed. It should be noted that, if one considers that limestone is the source of Ca in the clinker, this is an absolute limit. As it can be observed, the production of alite or belite-based clinkers will always result in CO2 emissions above 500 kg/ton of clinker, while the CSA, BYF and Solidia® cements allow a reduction of the CO2 process-related emissions below 400 kg/ton, keeping the same clinker production technology. Still, below the 400 kgCO2/ton of clinker, it is possible to find the alternatives X-Clinker and Celitement®, with both technologies being based on fully electrified processes. Concerning &#;wollastonitic&#; clinkers, two radically different approaches exist: the Solidia Cement approach, in which the setting of near-wollastonite phase specimens is achieved via carbonation, and the X-Clinker approach, in which instead of a crystalline material, the reactivity with water is achieved through the amorphization of the material with a composition close to wollastonite.
The direct emission of CO2 arising from materials decarbonation is an important factor but not the only one. In fact, the CO2 emissions arising from the firing process also play an important role in clinker production, which in the case of alite-, belite- and aluminate-based clinkers represent about 40% of the total CO2 emissions. In this way, the possibility of process electrification is also a key factor in what concerns the reduction of CO2 emissions in clinker production since this CO2 contribution could drop to zero if non-fossil sources are used for electric energy production. Under this scenario, the lower limit for the total CO2 emission would be defined by the own chemistry of each binder, as a result of the calcination of its raw materials.
presents a summary of the potential impact of each ACT regarding energy- and process-related CO2 emissions, as well as some important characteristics of the alternative technologies and binders. In this table, it was considered that the Celitement® clinkers are prone to electrification since they do not need a rotary kiln or considerably high temperature, which facilitates the implementation of resistive electrical or microwave heating. Likewise, the X-Clinker procedure does not implement a rotary and, even though there is the need for high temperatures, there is also a complete melting, which makes the overheating of the reaction media unproblematic in the production of clinker. Therefore, processes such as plasma heating or electrical arc are viable. All the other clinkers need a controlled high temperature and a rotary kiln, which makes the implementation of an electrification process challenging.
Conceptualization, R.C., R.B.H. and R.L.S.; methodology, R.C., M.A., R.L.S.; validation, R.C., J.P., P.R. and R.B.H.; formal analysis, R.C., R.B.H., J.P. and P.R.; investigation, M.A. and R.L.S.; data curation, M.A.; writing&#;original draft preparation, M.A. and R.L.S.; writing&#;review and editing, R.C., P.R., R.L.S. and M.A.; visualization, R.C., R.L.S. and M.A.; supervision, R.C., R.B.H. and R.L.S.; project administration, R.C. and P.R.; funding acquisition, R.C. All authors have read and agreed to the published version of the manuscript.
This work was supported by CIMPOR SGPS under contract CIMPOR/ADIST 006/ and, through Fundação para a Ciência e Tecnologia, under LAETA, project UIDB//.
The authors declare no conflict of interest.
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