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Retrofitting in Cement Plants for Emissions Reduction

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Gaseous emission – nitrogen oxides and sulphur oxides – can be reduced by making some changes to the existing installation.

The cement manufacturing process has undergone a lot of technological advancements with respect to product types, raw material and fuel types and improved automation and energy efficiency. Most of the emissions to the environment are in the form of particulates, carbon dioxide, nitrogen oxides and sulphur oxides in exhaust gases. In some countries, mercury emissions are monitored and controlled. In cases where fuel or raw material quality lead to higher emissions, end of pipe control technology can be applied to meet emission norms.

NOX formation in kiln flames is generally by both thermal and fuel routes (for coal, oil and petroleum coke). NOX formation takes place in the high temperature clinker burning process and the amount is directly related to the main flame temperature which is typically 1800 -2000?C. Thermal NOX is formed by the combination of atmospheric nitrogen and oxygen at very high temperatures. The reaction takes place between oxygen radicals, nitrogen radicals and molecular nitrogen. Apart from temperature, the in-flame oxygen concentration and the residence time in the high temperature zones influence the final thermal NOX emissions. Most fuels, other than gas, contain nitrogen bound as an organic compound in the structure. When the fuel is burnt this organic nitrogen becomes converted into a range of cyanide and amine species some of which are subsequently oxidised to NOX, depending on the local oxygen availability, but this mechanism is less dependent on temperature. Typical NOX emission values in older technologies can be as high as 1800-2000 mg/Nm3, while average emission values are around 1200 mg/Nm3 (based on 10% O2).

Sulphur is input into the clinker burning process via raw materials and fuels. Higher SO2 emissions by rotary kiln systems in the cement industry are due to sulphides contained in the raw material which become oxidised to form SO2 at the temperatures between 370 to 420?C prevailing in the kiln preheater. In some cases sulphur in fuel can also affect the emission of SO2. High values in the range of 600 to 800 mg/Nm3 have been observed.

Recently the norms for gaseous emissions from cement plants have undergone revision in India and the Ministry of Environment and Forests (MoEF) has amended the Environment (protection) Rules of 1986. The limits for NOX emissions for new plants are set at 600 mg/ Nm3 at 10%O2 (800 for older plants), and that for SO2 are set at 100 mg/Nm3 at 10% O2, dry basis. It will therefore be essential for producers to review their current operations to meet these new requirements, which are now quite stringent.

NOX emissions are dependent on certain process related factors such as

  • Feed mix composition
  • Kiln fuel type
  • Increased thermal efficiency
  • Burner Type

There are certain limits to which these factors can be optimised to reduce emissions while ensuring product quality and operational efficiency. As a result it becomes necessary to look at other solutions like retrofitting existing preheater, calciner or Tertiary Air TA duct to reduce the emissions.

For controlling NOX emissions the following retrofitting options can be incorporated in existing Preheater Precalciner type Dry cement Kilns.

Installing low NOX burners (LNB) in the kiln.
Two distinct combustion zones are created using LNBs. Flame turbulence and air and fuel mixing are suppressed during the first stage of combustion. A fuel-rich, oxygen-lean, high temperature combustion zone is created first by reducing the amount of primary air in the primary combustion zone and delaying the combustion of all of the fuel. A portion of the flue gas can be recycled into the primary combustion zone to reduce the oxygen content of the primary air.

At the high temperatures required to complete clinkering reactions, thermal NOX formation is suppressed in the primary combustion zone because less oxygen is available.

A secondary, oxygen-rich combustion zone follows, where fuel combustion is completed. Cooler secondary combustion air is mixed into the secondary combustion zone, lowering the temperature. Although excess oxygen is available, NOX formation is suppressed in the secondary combustion zone because of lower temperature. This method can secure to 10%-15% NOX reduction. However, the exact values will depend on the existing level of emissions.

Staged combustion in Calciner (SCC)
SCC works by staging the introduction of fuel, combustion air, and feed material in a manner to minimise NOX formation and reduce NOX to nitrogen. NOX formed in the kiln?s combustion zone is chemically reduced by maintaining a reducing atmosphere at the kiln feed end by firing fuel in this region. The reducing atmosphere is maintained in the calciner region by controlling combustion air such that the calcining fuel is first burned under reducing conditions to reduce NOX and then burned under oxidising conditions to complete the combustion reaction. However, the overall process parameters during kiln operation under such reducing conditions must be carefully watched to limit the CO emission, especially where ESP is being used instead of bag house.

Controlling the introduction of raw meal allows for control of the calciner temperature. Through these mechanisms, both fuel NOX and thermal NOX are controlled. The combustion chamber allows for improved control over the introduction of tertiary air in the calciner region, which helps to promote the proper reducing environment for NOX control.

The various technology providers achieve this staged combustion by different methods:

  • Staged air combustion in which along with delivery of the tertiary air to the calciner inlet, a portion of the tertiary air is delivered close to calciner outlet. Modification to the TA duct and calciner is required.
  • Staged air and fuel: Fuel is fired both in kiln riser and calciner and TA is delivered both at inlet of calciner and in the combustion zone close to the calciner outlet.
  • Sequenced Fuel and Air: This is the case of a typical Low NOX ILC system, where all fuel is fired in a reducing atmosphere near the kiln inlet, and tertiary air is supplied in the lower part of the calciner. Raw meal is split and introduced at different sections of the calciner. This type of calciner does not stage fuel or air, but instead injects all calciner fuel at the bottom of the calciner, before the kiln inlet. All tertiary air is introduced at a single point just above the fuel. A high-temperature reducing zone is created in the kiln riser duct, and the calciner is partially built into the kiln riser.

This method can secure to 25%-30% NOX reduction. However the exact values will depend on the existing level of emissions.

Selective Non-Catalytic Reduction
The SNCR process is basically the injection of ammonia in the form of ammonia water or urea in the flue-gas at a suitable temperature. An aqueous ammonia solution is the reagent that has been most often used for cement kilns, and experience indicates that an ammonia solution is most effective for PH/PC cement kiln applications. Other reagent alternatives include anhydrous ammonia (injected as a gas), urea solutions, and ammonium sulfate solutions. This reagent is called a reductant.

An SNCR system?s performance depends on

  • Residence time available in optimum temperature range
  • Degree of mixing between injected reagent and combustion gases
  • Uncontrolled NOX concentration level and Oxygen level
  • Molar ratio of injected reagent to uncontrolled NOX.

The SNCR system can be easily installed as retrofit in an existing pyroprocessing system. The following are the main additions

  • Reductant receipt and storage section. Adequate safety measures have to be taken for the handling of Ammonia solution or Ammonia.
  • The reductant pumping and delivery section
  • The reductant distribution system
  • The ammonia injection lances at calciner and/or kiln riser duct. The exact location and number of injection points will differ from one system to the next and are ptimised through testing.
  • Measurement equipment is necessary to maintain the appropriate ammonia feed rate and additional monitoring equipment is required to record the amount of NOx and ammonia slip in the gases exiting the SNCR system to adjust the amount of ammonia entering the system.
  • Temperature monitors are also required to make sure that the ammonia is delivered to the correct location.

Sometimes it may be necessary to use multiple reduction techniques so that the emission standards can be met. Due to the high operational cost of the system, SNCR should be used to the extent necessary only after achieving NOx reduction based on Process Optimisation and other retrofitting avenues described earlier in this paper. Similarly the SO2 emission from kilns are dependent on multiple factors, some of which can be optimised to reduce emissions. The following factors can be evaluated to optimise the SO2 emissions from cement kiln:

  • Inherent SO2 removal efficiency of the kiln system,
  • Limit raw material sulphur concentration and form of sulphur,
  • Raw mix design: The molecular ratio between sulphur (and chloride) and alkalis (sodium and potassium),
  • Whether oxidising or reducing conditions exist in the kiln system and where these conditions exist,
  • The temperature profile in the kiln system,
  • If an in-line raw mill is available and operating.
  • When the emission values cannot be improved by process optimisation alone, it becomes necessary to adopt suitable secondary measures. Some of the retrofit solutions are described below.

Lime Addition to Kiln Feed
Lime Addition to Kiln Feed consists of mixing lime (CaO) with the raw Kiln feed. The CaO would react with SO2 driven off in the kiln to form calcium sulfite (CaSO3) and calcium sulfate (CaSO4). The reactions can occur in the calciner, throughout the rotary kiln, and in the lower stages of the flash calciner (i.e., at any location in the system at which CaO and SO2 are present simultaneously and are mixed adequately). The amount of SO2 absorbed through this mechanism at any location in the pyroprocess is dependent on the site-specific temperature and other factors such as the time of contact between the reactants. Once sulfur is absorbed as CaSO4 in the materials in the pyroprocess, it is unlikely to be released again as SO2. CaSO4 would be retained in the raw mix and ultimately be converted into clinker.

Installation of SOX reduction cyclone
SO2 formed in the upper cyclone stages of the preheater can be reduced by reaction with the naturally occurring CaO present in the pyro system. CaO is formed in the calciner, and gas and dust containing high amounts of CaO can be directed to the upper stages for SO2 reduction by a minor calciner modification.

This SO2 removal system consists of a low pressure cyclone, with inlet outlet ducts, a material feed pipe, sluice flap and distribution box. The inlet duct conveys gas from the inline calciner to the SO2 collecting cyclone. The outlet duct conveys gas to the Stage two or three inlet duct. A material feed pipe is provided for the SO2 collecting cyclone and will terminate at stage below top stage or top stage distribution box. This system uses the differential pressure across the preheater tower to provide the driving force to convey the calcined material from the bottom to top.

Upto 35% control of SO2 is possible depending on existing situation in the kiln.

Dry Sorbent Injection
Dry Sorbent Injection (DSI) utilises finely ground sorbent which is injected in the gas stream of the kiln. The sorbent typically used is a hydrated lime, sodium bicarbonate or Trona (soda ash). Water may be injected separately from the sorbent either downstream or upstream of the dry sorbent injection point to humidify the flue gas. The relative position of the dry sorbent and water injection is optimised to promote maximum droplet scavenging or impacts between sorbent particles and water droplets, both suspended in the gas stream. Fly ash, reaction products, and any unreacted sorbent are collected in the particulate control device. Some extent of dry scrubbing is inherent in the preheater tower.

Upto 60% control of SO2 is possible depending on the amount of lime that is fed into the kiln.

Wet Lime Scrubbing
This is based on the reaction between Ca(OH)2 and SO2 with a lime slurry is introduced as a mist into a gas stream containing SO2. The mole ration of Ca(OH)2 to SO2 is usually 2:1. This slurry can be introduced in the existing Gas Conditioning tower located between preheater and in-line raw mills. The lime spray can be modulated depending on kiln operating conditions such as when raw mill is not in operation.

Upto 90% control of SO2 is possible depending on the existing system and improvement required. However the handling of such systems with the cement plant entails higher operation and maintenance costs. Hence the wet and semi-dry processes are not deployed unless the emissions are exceptionally high.

Engineering consultants like ERCOM, who have a global experience, have already assisted their customers abroad in achieving stringent emission limits. A quick and efficient technical audit can be carried for existing cement plants to check the likely compliance levels with respect to the new MoEF Notification. By assisting plants in carrying out process optimisation, we can help reduce the emissions with primary measures. In order to achieve further reductions, we can help clients in selecting the appropriate cost effective retrofit solution. Plant modifications for reduction of emission can be evaluated by us and we can aid in timely implementation with minimum disturbance to plant operation. Together with technology providers and cement plant owners, we can go a long way in paving the path for sustainable and environment friendly cement production.

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Concrete

Balancing Demand and Sustainability

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ICR discusses India’s rapid advances in renewable energy, on track to exceed its 2030 targets, even as the rising energy demands challenge complete reliance on sustainable sources.

The cement industry, a cornerstone of infrastructure development, has long been associated with high emissions, particularly of CO2. This sector alone is responsible for approximately 8 per cent of global carbon dioxide emissions, primarily due to the energy-intensive processes of clinker production and calcination. Beyond carbon emissions, cement production also generates particulates, nitrogen oxides (NOx), sulphur oxides (SOx), and other pollutants, contributing to environmental degradation and health risks. With the global push towards sustainable practices and carbon neutrality, addressing emissions in the cement industry has become imperative.
According to Climate Change Performance Index, India ranks 7 in 2024. India receives a high ranking in the GHG Emissions and Energy Use categories, but a medium in Climate Policy and Renewable Energy, as in the previous year. While India is the world’s most populous country, it has relatively low per capita emissions. Data shows that in the per capita GHG category, the country is on track to meet a benchmark of well below 2°C.
India’s situation underscores the complexity of transitioning to sustainable energy systems in the face of rising and fluctuating energy needs. International support is crucial for India to access advanced technologies, financial resources, and best practices that can accelerate its transition to a sustainable energy future. Our analysis shows that with current policies, India will overachieve its conditional NDC targets of achieving 50 per cent non-fossil capacity by 2030, so it could set stronger targets. India has ambitious renewable energy plans as outlined in the National Electricity Plan 2023 (NEP2023) aiming for a share of installed capacity of 57 per cent and 66 per cent in 2026-27 and 2031-32, respectively. Share of renewable energy capacity in India reached 44 per cent, ranked fourth in the world in renewable energy capacity installations in 2023, after China, the US and Germany. The NEP2023 is reflected in the lower bound of our current policy and action pathway.
India has seen a steady increase in renewable energy deployment, including both utility-scale and rooftop solar, leading to the share of coal capacity dropping below 50 per cent for the first time. However, this increase in renewable energy capacity is barely able to keep up with the surging demand. As a result, the electricity generation share of renewable energy, including large hydro, remains at around 18 per cent, showing no improvement since last year. Investment in renewable energy projects in India are projected to increase by over 83 per cent to around USD 16.5 bn in 2024, with fossil fuel companies also diversifying their investments into the renewable sector. Despite this, India has not committed to phasing out coal power or fossil gas.
The National Electricity Plan indicated a temporary halt in coal capacity addition, but current under-construction capacity exceeds the threshold stated in these plans. While new gas power projects have been abandoned, the utilisation of existing gas power plants has increased to meet energy demand driven by severe heat stress.

Understanding Emissions in Cement Production
Primary Sources of Emissions: Cement production emissions stem mainly from three sources: calcination, fuel combustion, and electricity use. During calcination, limestone is heated to produce clinker, releasing CO2 as a by-product. This process alone accounts for roughly 60 per cent of emissions in cement manufacturing. The remaining emissions result from burning fossil fuels in kilns to achieve the high temperatures needed for calcination and from electricity consumption across production stages.
Raju Ramchandran, SVP Manufacturing (Cluster Head – Central), Nuvoco Vistas, says, “We consistently track air emissions from fuel combustion in our cement manufacturing and power generation operations. The burning of fossil fuels releases pollutants such as Oxides of Sulphur (SOx), Oxides of Nitrogen (NOx), and Particulate Matter (PM), which require stringent monitoring.”
“We ensure compliance with regulatory standards by using the Continuous Emission Monitoring System (CEMS) to monitor these emissions. For the FY 23-24, both our stack and fugitive emissions have stayed within the permissible limits set by Pollution Control Boards. Moreover, our ongoing monitoring of fugitive emissions ensures that we meet the prerequisite air quality standards,” he adds.
In addition to CO2, the cement industry releases various pollutants that pose risks to air quality and public health. These include particulate matter, NOx, and SOx, which can lead to respiratory and cardiovascular issues, acid rain, and ecosystem imbalances.
Governments worldwide are setting increasingly stringent regulations to curb industrial emissions. Standards such as the EU Emissions Trading System and India’s National Action Plan on Climate Change encourage cement manufacturers to adopt cleaner technologies. Many countries now impose limits on NOx, SOx and particulate emissions, with the aim of minimising the industry’s environmental impact.

Challenges in Reducing Emissions
High carbon intensity of cement production: Cement’s high carbon intensity largely stems from the chemical reactions involved in transforming limestone into clinker, making emissions difficult to reduce without altering core processes. Additionally, achieving the necessary kiln temperatures requires significant energy, often derived from coal or natural gas.
Operational limitations: Altering the traditional cement production process can compromise the quality and durability of the end product. Adapting existing production lines for lower emissions involves extensive R&D and technical trials to ensure the finished cement meets industry standards.
Financial constraints: The cost of implementing green technology is high, creating economic challenges, particularly for smaller cement manufacturers. Equipment upgrades, energy-efficient kilns, and carbon capture facilities require considerable investment, which many companies find difficult to justify without strong financial incentives.
Balancing market demands and environmental goals: With global infrastructure demands rising, the cement industry faces pressure to meet growing production needs while simultaneously working to reduce emissions. Balancing these competing demands requires innovation, efficient resource management, and support from stakeholders.

Technological Innovations for Emission Reduction
Alternative fuels and energy sources: One of the most effective ways to reduce emissions is by replacing fossil fuels with alternatives like waste-derived fuels, biomass, or biofuels. Some manufacturers are incorporating solar and wind energy to power auxiliary processes, further reducing reliance on traditional energy sources.
Sudhir Pathak, Head- Central Design & Engg (CDE), QA, Green Hydrogen, Hero Future Energies, says, “The cement industry is one of the largest consumers of grid power (Scope 2) and also a guzzler of in-process fossil CO2 (Scopem1) including process-based CO2 through limekilns. Decarbonisation can be achieved only up to 50 per cent to 60 per cent through plain hybrid solar and wind. However, for achieving balance 40 per cent, storage is essential, be it chemical or mechanical. Today, HFE is ready to provide such bespoke storage solutions as is evident through several complex RTC tenders that we have won in the last 6-8 months floated by agencies like SECI, NTPC and SJVN. These include tenders for FDRE projects, peak power, load following, etc. Further, regarding green hydrogen and its derivatives, we are ready to apply these for decarbonising industrial heating and mobility.”
Carbon Capture and Storage (CCS): CCS technology captures emissions at the source, storing CO2 to prevent it from entering the atmosphere. Recent advancements in CCS technology make it a viable option for large-scale cement plants, although high costs and infrastructure requirements remain obstacles to widespread adoption.
Clinker Substitution: Reducing clinker content is a promising method for emission reduction, achieved by using supplementary cementitious materials (SCMs) such as fly ash, slag, and calcined clay. These materials not only reduce CO2 emissions but also enhance the durability and performance of cement. SCMs are gradually becoming industry-standard components, especially in eco-friendly and green cement products.
Rajesh Kumar Nayma, Assistant General Manager – Environment, Wonder Cement, says, “The use of AFR plays a critical role in our strategy to reduce the environmental footprint of cement production. By substituting traditional fossil fuels with waste-derived alternatives like biomass, refuse-derived fuel (RDF) and industrial by-products, we significantly lower CO2 emissions and reduce the demand for natural resources. The utilisation of supplementary cementitious materials (SCMs), such as fly ash, helps in reducing clinker consumption, which is a major source of carbon emissions in cement production. This not only decreases our reliance on energy-intensive processes but also promotes waste recycling and resource efficiency. AFR adoption is an integral part of our commitment to the circular economy, ensuring that we minimise waste and optimise the use of materials throughout the production cycle, ultimately contributing to a more sustainable and eco-friendly cement industry.”
“WCL is exploring transitioning from fossil fuels to cleaner alternatives like biofuels or hydrogen or RDF/plastic waste/other hazardous waste. Till date, 5 per cent TSR has been achieved, while the intent is to achieve more than 20 per cent TSR. WCL is utilising the hazardous and other waste as an alternative fuel or raw material. We have used more than 3 lakh metric tonne of hydrogen waste and other waste in FY-2023-24,” he adds.
Improving energy efficiency is critical for emissions reduction. Technologies like high-efficiency kilns, heat recovery systems, and process optimisation techniques are helping manufacturers achieve more output with less energy. These measures reduce the carbon footprint while lowering operational costs.

The Role of SCMs
SCMs serve as partial replacements for clinker, providing a dual benefit of reduced carbon emissions and improved product resilience. The use of materials like fly ash and slag also helps mitigate industrial waste, contributing to a circular economy. Fly ash, slag, and silica fume are among the most widely used SCMs. Each has unique properties that contribute to cement’s strength, workability, and durability. By incorporating SCMs, manufacturers can produce cement with a lower environmental footprint without compromising quality.
While SCMs are effective, several obstacles hinder their widespread adoption. Supply chain constraints, material variability, and lack of technical standards are challenges that manufacturers face. Additionally, geographic limitations impact access to certain SCMs, creating disparities in their usage across regions.

Policy and Industry Collaboration
Policies play a critical role in driving green transitions within the cement industry. Carbon credits, tax incentives, and funding for R&D are some measures governments have introduced to support emission reduction. India’s Perform, Achieve, and Trade (PAT) scheme is an example of a policy incentivising industrial energy efficiency.
Collaborations between government entities, private corporations, and research institutions foster innovation and accelerate the adoption of sustainable practices. Partnerships can also help address funding gaps, allowing companies to explore new technologies without bearing the full financial burden.
International frameworks such as the Paris Agreement and industry-led efforts like the Global Cement and Concrete Association (GCCA) are setting targets for sustainable cement production. These initiatives encourage the sector to adopt environmentally friendly practices and set a roadmap toward achieving net-zero emissions.

Towards a Net-Zero Future
Reaching net-zero emissions is an ambitious but necessary goal for the cement industry. Realistic targets, set with interim milestones, allow companies to gradually transition to greener processes while maintaining production efficiency. Continued investment in R&D is crucial for discovering new methods of emission reduction. Emerging technologies such as carbon-negative materials, alternative binders, and low-carbon clinkers hold promise for the future, potentially transforming cement production into a more sustainable process.
Increasingly, consumers and investors are prioritising sustainability, placing pressure on companies to reduce their environmental impact. This shift in consumer sentiment is driving the cement industry to adopt green practices and focus on transparency in emissions reporting.

Conclusion
The journey toward reducing environmental impact in the cement industry is complex and multifaceted, requiring a combination of innovation, policy support, and industry collaboration. By adopting alternative fuels, implementing carbon capture technology, integrating SCMs, and improving energy efficiency, the industry can take significant strides in minimising its carbon footprint. Achieving sustainability in cement production is essential not only for the industry’s future but also for the planet’s well-being. Together, industry players, policymakers, and consumers can support the transition to a net-zero future, ensuring that cement remains a vital yet sustainable component of global infrastructure.

– Kanika Mathur

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Concrete

Red River Formation in Kiln Operations

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Dr SB Hegde, Professor, Jain College of Engineering and Technology, Hubli, and Visiting Professor, Pennsylvania State University, USA, helps us understand the red river formation in cement kiln operations, its causes, impacts and mitigation strategies.

Red river formation in cement kilns, where molten clinker flows uncontrollably in the cooler, is a costly problem for cement plants. The phenomenon not only affects clinker quality but also leads to significant operational disruptions, increased energy consumption and accelerated wear on kiln refractory bricks. Understanding the factors that cause red river formation and implementing strategies to prevent it are critical to maintaining operational efficiency and clinker quality.
This paper explores the causes of red river formation, the operational impacts it has on kiln performance, and the various mitigation strategies that cement plants can adopt. Additionally, safety considerations associated with the prevention and handling of red river formation are discussed, with practical insights from case studies of successful plant interventions in India and globally.

Causes of red river formation
Red river formation is primarily caused by improper kiln operations, including fluctuating kiln temperatures, oxygen levels, and cooler inefficiency. The following parameters are essential contributors:
Kiln temperature: Inconsistent temperature control in the kiln’s burning zone, often exceeding 1500°C, creates an imbalance between the solid and molten clinker phases, leading to red river formation. Maintaining temperatures within a more stable range of 1470-1490°C ensures that the clinker remains solid as it moves into the cooler.
Oxygen levels and CO concentrations: Oxygen levels above 2.5 per cent increase the risk of over-combustion, while elevated CO levels above 0.3 per cent indicate incomplete combustion, both contributing to excessive clinker melting. Optimising oxygen levels to 1.8-2.0 per cent minimises the risk.
Raw mix composition: The raw mix plays a vital role in clinker formation. A high liquid phase due to improper ratios of silica, alumina, and iron oxide can lead to excessive melting. Controlling the silica modulus (SM: 2.3-2.7) and alumina modulus (AM: 1.3-1.8) ensures a more stable clinker and reduces the risk of red river formation. If the raw mix is improperly proportioned, red river formation becomes more likely due to high fluxing compounds that melt at lower temperatures.
Kiln speed and torque: Kiln speeds that fluctuate below 3.4 rpm can cause material buildup, while kiln torque exceeding 50-60 per cent indicates stress that can lead to clinker instability.
Cooler efficiency: Inefficiencies in the clinker cooler, with efficiency levels below 78 per cent, can exacerbate red river formation. Clinker that is not cooled properly will remain molten for longer, allowing it to flow uncontrollably. Coolers should maintain exit temperatures between 180-200°C to prevent red river incidents.
Impact on clinker quality and kiln performance
The occurrence of red river has numerous negative impacts on both clinker quality and kiln performance:
Clinker quality: Red river formation results in poor clinker grindability, higher variability in free lime content and inconsistent cement properties. Poor clinker reactivity reduces both early and late strength development in the final cement product.
Increased heat consumption: Red river typically increases specific heat consumption by 3-5 per cent, resulting in higher fuel usage. These inefficiencies can significantly affect the plant’s cost structure, driving up operational expenses.
Refractory damage: The molten clinker accelerates the wear of refractory bricks in the kiln, especially in the burning zone and cooler transition areas. Brick life can decrease by 25-30 per cent, leading to more frequent replacements and higher maintenance costs.
Equipment and instrumentation damage: The uncontrolled molten flow of clinker during red river incidents can damage cooler plates, kiln discharge systems, and even temperature sensors and thermocouples, leading to costly repairs and prolonged downtime.

Mitigation strategies
Mitigating red river formation requires a multi-faceted approach combining operational optimisation, automation and staff training:
Kiln temperature control: Maintaining stable burning zone temperatures in the 1470-1490°C range is key to preventing excessive melting of clinker. Advanced temperature monitoring systems can help regulate temperature fluctuations.
Cooler efficiency optimisation: To ensure proper cooling, cooler efficiency must be maintained at 78-80 per cent, with clinker exit temperatures not exceeding 200°C. Real-time airflow adjustments in grate coolers improve cooling performance, solidifying the clinker at the appropriate stage.
Automation and data analytics: Advanced Process Control (APC) systems using data analytics can monitor critical kiln parameters—such as temperature, oxygen levels, and torque—in real-time, allowing for predictive maintenance and early intervention when red river signs appear. This technology has been implemented successfully in leading plants globally to prevent red river formation.

Indian case studies
Case Study 1: Cement Plant in South India – Optimisation of Kiln Parameters
A cement plant in South India faced recurrent red river issues due to high kiln temperatures and low cooler efficiency. After comprehensive process audits, the plant optimised its kiln temperature to 1480°C, reduced oxygen levels to 1.9 per cent, and upgraded its cooler to an efficiency of 80 per cent. These changes reduced red river incidents by 85 per cent, saving the plant Rs 10 million in energy costs annually and improving clinker quality by
15 per cent.

Case Study 2: Cement Plant in North India – Cooler Upgrade and Automation
A northern India plant increased cooler efficiency from 70 per cent to 78 per cent by installing an advanced grate cooler. This reduced clinker exit temperatures to 190°C, preventing red river formation. Automation systems provided real-time adjustments, decreasing the frequency of incidents by 75 per cent and saving `12 million annually.

Global Case Studies
Case Study 1: European Plant – Automation Success
A German cement plant, experiencing red river issues due to fluctuating oxygen levels, installed an advanced data-driven automation system. The system stabilised oxygen at 1.9 per cent and maintained kiln temperature at 1,475-1,485°C, reducing red river by 90 per cent. Clinker quality improved by 10 per cent, with a reduction in specific heat consumption by 4 per cent.

Case study 2: US Plant – Operator Training and Process Optimisation
A US cement plant reduced red river occurrences by 70 per cent through kiln speed optimisation (3.8 rpm) and comprehensive operator training. Improved monitoring of kiln torque and cooler exit temperatures led to higher cooler efficiency (75 per cent) and an annual savings of $2 million.

Safety Aspects
Safety is a paramount concern in red river incidents. When molten clinker flows uncontrollably, it poses a significant risk to personnel working near the kiln and cooler areas.

To mitigate these risks:

  • Clearance zones: Kiln and cooler areas should have strict clearance zones for personnel when red river incidents are detected.
  • Protective gear and training: Personnel should be equipped with proper protective equipment (PPEs) and trained to handle emergencies involving molten clinker. Emergency shutdown procedures should be well-documented and rehearsed.
  • Automation and early warning systems: Automation can provide early warning systems that alert operators to potential red river formation before it becomes critical, ensuring safe intervention.

Conclusion
Red river formation remains a major operational challenge for cement plants, but it can be effectively mitigated through proper kiln temperature control, cooler efficiency optimisation and the use of advanced automation systems.
The case studies highlight the importance of process improvements and staff training in reducing red river occurrences, improving clinker quality, and lowering operational costs. Additionally, safety
measures must be prioritised to protect personnel from the risks posed by molten clinker. By incorporating these strategies, cement plants can ensure consistent kiln performance and enhanced operational efficiency.

References
1. Duda, W. H. (1985). Cement Data Book. International Process Engineering in the Cement Industry. Bauverlag GmbH.
2. Javed, I., & Sobolev, K. (2020). “Use of Automation in Modern Cement Plants.” Cement and Concrete Research, 130, 105967.
3. Tamilselvan, P., & Kumar, R. (2023). “Optimisation of Kiln and Cooler Systems in Indian Cement Plants.” Indian Cement Review, 34(7), 42-48.
4. Martin, L. (2019). “Case Studies of Red River Mitigation in European Cement Plants.” International Journal of Cement Production, 12(2), 63-78.
5. Schorr, H. (2021). “Advanced Process Control in Cement Manufacturing.” Cement International, 19(3), 30-37.
6. Singh, V. K., & Gupta, A. (2022). “Impact of Raw Mix on Clinker Formation and Kiln Operations.” Global Cement Magazine, 14(4), 22-29.

About the author: Dr SB Hegde brings over thirty years of leadership experience in the cement industry in India and internationally. He has published over 198 research papers and holds six patents, with four more filed in the USA in 2023. His advisory roles extend to multinational cement companies globally and a governmental Think Tank, contributing to research and policy. Recognised for his contributions, he received the ‘Global Visionary Award’ in 2020 from the Gujarat Chambers of Commerce and Industry.

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SCMs encourage closed-loop systems

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As the cement industry prioritises sustainability and performance, Supplementary Cementitious Materials (SCMs) are redefining standards, explains Tushar Khandhadia, General Manager – Production, Udaipur Cement Works.

What role do supplementary cementitious materials (SCMs) play in enhancing the performance and sustainability of cement and concrete?
SCMs play a crucial role in enhancing the performance and sustainability of cement and concrete. These materials are added to concrete to improve its properties such as strength, durability, and workability, as well as to reduce the environmental impact of cement production. The addition of SCMs to cement reduces the amount of Portland cement required to manufacture concrete, reducing the carbon footprint of the concrete. These materials are often industrial waste products or by-products that can be used as a replacement for cement, such as fly ash, slag and silica fume.
SCMs also reduce the amount of water required to produce concrete, which reduces the environmental impact of concrete production. This is achieved through their ability to improve the workability of concrete, allowing the same amount of work to be done with less water.
In addition, SCMs improve the durability of concrete by reducing the risk of cracking and improving resistance to chemical attack and other forms of degradation.

How has your company integrated SCMs into its production process, and what challenges have you encountered?
The integration of SCMs into cement and concrete production may pose certain challenges in the areas of sourcing, handling and production optimisation.

  • Sourcing: Finding an adequate and reliable supply of SCMs can be a challenge. Some SCMs, such as fly ash and slag, are readily available by-products of other industrial processes, while others such as silica fume or metakaolin may be more difficult to source.
  • Handling: The storage, handling, and transportation of SCMs require special considerations due to their physical and chemical properties. For instance, some SCMs are stored in moist conditions to prevent them from drying out and becoming airborne, which could pose a safety risk to workers.
  • Production optimisation: The addition of SCMs into the mix may require adjustments to the production process to achieve the desired properties of cement and concrete. For example, the use of SCMs may affect the setting time, workability, strength gain, and other properties of the final product, which may require reconfiguration of the production process.
  • Quality control: The addition of SCMs may introduce variability in the properties of cement and concrete, and rigorous quality control measures are necessary to ensure the final product meets the required specifications and standards.

Proper planning, handling and production optimisation are essential in overcoming the challenges encountered during the integration process.

Can you share insights on how SCMs such as fly ash, slag and silica fume impact the durability and strength of concrete in different environmental conditions?

  • Fly ash is a by-product of coal combustion and is widely used as an SCM in the production of concrete. When added to concrete, fly ash reacts with the calcium hydroxide present in the concrete to form additional cementitious materials, resulting in improved strength and durability. Fly ash increases the durability of concrete by improving its resistance to sulphate and acid attacks, reducing shrinkage and decreasing the permeability of concrete. Fly ash also enhances the workability and pumpability of concrete while reducing the heat of hydration, which reduces the risk of thermal cracking. In cold climates, fly ash helps to reduce the risk of freeze-thaw damage.
  • Slag is a by-product of steel production and is used as an SCM because of its high silica and alumina content. When added to concrete, slag reacts with the calcium hydroxide present in the concrete to form additional cementitious materials, resulting in improved strength and durability. Slag increases the durability of concrete by improving its resistance to sulphate and acid attacks, reducing shrinkage and improving the strength of concrete over time. Slag also enhances the workability of concrete, reduces the heat of hydration, and improves the resistance of concrete to chloride penetration.
  • Silica fume is a by-product of the production of silicon and ferrosilicon alloys and is used as an SCM because of its high silica content. When added to concrete, silica fumes react with the calcium hydroxide present in the concrete to form additional cementitious materials, resulting in improved strength and durability. Silica fume increases the durability of concrete by improving its resistance to sulphate and acid attacks, reducing permeability, and improving abrasion resistance. Silica fume also enhances the workability of concrete, reduces the heat of hydration, and improves the resistance of concrete to chloride penetration.

Overall, the use of SCMs such as fly ash, slag and silica fume can significantly improve the durability and strength of concrete in different environmental conditions. Their impact on concrete varies depending on the availability, physical and chemical properties of the specific SCM being used and proper testing and engineering analysis should be done for each mix design in order to optimise the final product.

With the global push for sustainability, how do SCMs contribute to reducing the carbon footprint of cement production?
SCMs provide an environmentally friendly alternative to traditional Portland cement by reducing the amount of clinker required to produce cement. Clinker is the main ingredient in Portland cement and is produced by heating limestone and other raw materials to high temperatures, which releases significant GHG emissions. Thus, by using SCMs, less clinker is required, thereby reducing GHG emissions, energy use and the environmental impact of cement production. Some SCMs such as fly ash and slag are by-products of other industrial processes, meaning that their use in cement production reduces waste and enhances resource efficiency. Moreover, the use of SCMs can enhance the properties of concrete, thereby increasing its durability and service life which helps to further reduce the overall embodied carbon of the structure.
In short, the use of SCMs contributes to reducing the carbon footprint of cement production by improving the efficiency of resource utilisation and reducing greenhouse gas (GHG) emissions during the production process. This has led to an increased demand for SCMs in the construction industry, as environmental concerns and sustainable development goals have become more prominent factors in the selection of building materials.

What strategies or innovations has your company adopted to ensure a consistent and reliable supply of SCMs, given their reliance on industrial by-products?

  • Developing partnerships with suppliers: Many cement and concrete manufacturers establish long-term partnerships with suppliers of SCMs. These partnerships provide a reliable supply of high-quality SCMs, improve supply chain efficiency, and often provide access to new sources of SCMs.
  • Advanced SCM processing techniques: Many companies are investing in advanced processing techniques to unlock new sources of high-quality SCMs. Advanced processing techniques include new separation processes, calcination techniques, and chemical activation methods.
  • Alternative SCM sources: Many companies are exploring alternative SCM sources to supplement or replace traditional SCMs. Examples include agricultural by-products such as rice hull ash or sugar cane bagasse ash, which can be used in place of fly ash.
  • Quality control measures: Strict quality control measures are necessary to ensure consistent quality of SCMs. Many companies use advanced testing methods, such as particle size analysis, chemical analysis, and performance testing, to validate the quality of SCM materials used in production.
  • Supply chain diversification: Diversifying suppliers and SCM sources is another way to ensure a reliable supply. This reduces the risk of supply chain disruptions caused by factors such as natural disasters, market changes, or geopolitical risks.

The strategies and innovations adopted to ensure a consistent and reliable supply of SCMs include establishing long-term partnerships with suppliers, investing in advanced processing techniques, exploring alternative SCM sources, implementing strict quality control measures, and diversifying supply chains. By implementing these approaches, we ensure that use of SCMs in cement production is an effective and viable solution for reducing the environmental impact of operations

How does the use of SCMs align with your company’s broader goals around circular economy and resource efficiency?
Here are some ways in which the use of SCMs supports these goals:

  • Reducing waste: The use of SCMs, such as fly ash and slag, diverts significant quantities of industrial waste from landfills, turning it into a valuable resource that can be used in construction. This helps to reduce waste and conserve natural resources.
  • Reducing carbon emissions: Cement production is a significant contributor to greenhouse gas emissions, and the use of SCMs can significantly reduce the amount of cement required in concrete mixtures. This helps to reduce the carbon footprint of construction activities and move towards a low-carbon economy.
  • Enhancing resource efficiency: The use of SCMs can reduce the demand for raw materials, energy, and water in the production of concrete. This not only conserves natural resources but also reduces the costs associated with the extraction, transportation and processing of these materials.
  • Closing the loop: SCMs encourage closed-loop systems in the construction sector, where waste materials from one process become input materials for another. This can improve the efficiency and sustainability of the construction industry.
  • Supporting sustainable design practices: The use of SCMs can support sustainable design practices by improving the durability and performance of structures while also reducing their environmental impact. This supports a circular approach to design, construction and operation of buildings and infrastructure
    that improves their social, economic and environmental sustainability.

What future trends or developments do you foresee in the use of SCMs within the cement industry?
Future trends in the use of SCMs within the cement industry are likely to focus on: increased utilisation of diverse waste-derived SCMs, development of new SCM sources to address potential shortages, advanced characterisation techniques to optimise SCM blends and data-driven approaches to predict and optimise SCM usage for reduced carbon footprint and improved concrete performance; all driven by the growing need for sustainable cement production and stricter environmental regulations.
Key aspects of this trend include:

  • Expanding SCM sources: Exploring a wider range of industrial byproducts and waste materials like recycled concrete aggregate, activated clays and certain types of industrial minerals as potential SCMs to reduce reliance on traditional sources like fly ash, which may become increasingly limited.
  • Advanced material characterisation: Utilising sophisticated techniques to better understand the chemical and physical properties of SCMs, allowing for more precise blending and optimisation of their use in cement mixtures.
  • Data-driven decision making: Implementing machine learning and big data analysis to predict the performance of different SCM combinations, allowing for real-time adjustments in cement production based on available SCM sources and desired concrete properties.
  • Focus on local sourcing: Prioritising the use of locally available SCMs to reduce transportation costs and environmental impact.
  • Development of new SCM processing techniques: Research into methods to enhance the reactivity and performance of less readily usable SCMs through processes like activation or modification.
  • Life cycle analysis (LCA) integration: Using LCA to assess the full environmental impact of different SCMs and optimise their use to minimise carbon emissions throughout the cement production process.
  • Regulatory frameworks and standards:Increased adoption of building codes and industry standards that promote the use of SCMs and set targets for reduced carbon emissions in cement production.

– Kanika Mathur

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