Meknes Kiln 1 Tertiary Air Duct Dust Accumulation Probl

Meknes Kiln Tertiary Air Duct Dust: Complete Guide & Downloa

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Meknes Kiln Tertiary Air Duct Dust: Complete Guide & Downloa – Complete Cement Technical Package


Meknes Kiln Tertiary Air Duct Dust: Complete Guide & Downloa

The tertiary air duct is the pipe that carries the hot combustion air from the clinker cooler to the calciner and the burner, and it is one of the critical gas paths of the modern kiln system with a precalciner. The tertiary air duct operates in the environment of the hot gas, the dust-laden atmosphere and the high velocities, and the dust accumulation in the tertiary air duct is one of the most common operational problems of the kiln systems: the deposits build up on the duct walls, the effective cross-section narrows, the air flow is restricted, the combustion conditions in the calciner are disturbed, the heat consumption rises and the production suffers, and in the severe cases the duct is blocked and the kiln system must be stopped. This article addresses the tertiary air duct dust accumulation problem in the professional depth: the function and the design of the tertiary air duct, the mechanisms of the dust accumulation, the causes in the operation and the process, the symptoms and the detection, the consequences for the kiln system, the prevention by the design and the operation, the cleaning methods, and the engineering solutions for the existing and the new plants. The article is written in the generic technical form that applies to any kiln system facing this problem, and its objective is to give the process and the mechanical engineers, the operators and the plant management the complete understanding and the practical toolbox for the diagnosis, the prevention and the solution of the tertiary air duct dust accumulation problems.

The Function and the Design of the Tertiary Air Duct

The tertiary air is the air that is taken from the clinker cooler and delivered to the calciner and the kiln burner: the cooler exhaust air is hot and oxygen-rich, the tertiary air duct carries it from the cooler to the calciner, where it provides the oxygen for the calciner fuel combustion, and to the burner, where it supports the kiln combustion. The tertiary air duct is the connection that balances the air distribution of the kiln system: the primary air, the secondary air and the tertiary air split the combustion air between the burner and the calciner, and the tertiary air share is typically 40 to 60 percent of the total combustion air in the precalciner systems.

The tertiary air duct is designed for the hot and the dusty air: the duct diameter is set by the air flow and the velocity, the duct length connects the cooler to the calciner with the defined routing, the duct is insulated and lined to limit the heat loss and to protect the steel, and the duct is equipped with the dampers, the butterfly or the slide valves, which control the air flow. The duct velocity is a critical design parameter: the velocity must be high enough to carry the dust and to prevent the deposition, typically in the range of 15 to 25 meters per second, and the velocity must be low enough to limit the pressure drop and the erosion, and the design velocity is the balance of the two requirements. The duct routing includes the horizontal, the inclined and the vertical sections, the bends and the transitions, and the routing affects the dust behavior: the horizontal and the low-velocity sections are the sections where the dust settles.

The tertiary air duct interfaces with the kiln system at the three ends: at the cooler, the duct takes the hot air from the cooler chamber or the hood, at the calciner, the duct enters with the defined inlet geometry, and along the route, the duct passes through the tower and the structural supports. The interface conditions determine the dust load of the tertiary air: the cooler air carries the dust from the clinker, the grate and the air distribution, and the tertiary air dust load is one of the design inputs of the duct and the calciner. The tertiary air temperature is in the range of 800 to 1000 degrees Celsius in the normal operation, and the temperature is the factor that governs the deposition chemistry, the alkali and the sulfate condensation, and the thermal expansion of the duct.

The design of the tertiary air duct is the first line of the dust accumulation prevention: the velocity, the routing, the bends, the dampers and the cleaning provisions are the design variables, and the professional design practice addresses the dust accumulation from the design stage. The existing plants face the design limitations, and the engineering solutions for the existing plants are the retrofit measures that the article covers in the later sections.

The Mechanisms of the Dust Accumulation

The dust accumulation in the tertiary air duct is the result of the interaction of the dust, the gas and the wall, and the understanding of the mechanisms is the foundation of the diagnosis and the prevention. The main mechanisms are the inertial deposition, the turbulent deposition, the condensation and the adhesion, and the mechanisms combine in the different proportions depending on the conditions.

The inertial deposition is the deposition of the coarse dust particles on the duct surfaces: the particles that cannot follow the gas flow, the particles with the inertia, leave the flow at the bends, the transitions, the dampers and the obstructions, and they impact the walls and the surfaces. The inertial deposition is strongest at the bends, where the flow changes the direction and the particles continue straight, at the dampers, where the flow accelerates and the particles impact the damper and the seats, and at the transitions and the obstructions, where the flow is disturbed. The inertial deposition is the mechanism of the local deposits: the deposits grow at the impact zones, the deposits narrow the flow, the velocity increases at the deposits and the deposition accelerates, which is the self-accelerating mechanism of the dust accumulation.

The turbulent deposition is the deposition of the fine particles from the turbulent flow: the turbulence carries the particles to the wall region, the particles diffuse through the boundary layer and deposit on the wall, and the deposition rate depends on the particle size, the turbulence intensity and the wall conditions. The turbulent deposition is the mechanism of the uniform deposits: the deposits grow on the duct walls along the length, the deposits are thinner than the inertial deposits, and the deposits are the layer that the high-velocity flow partially removes and that the low-velocity flow allows to grow.

The condensation is the deposition of the volatile components: the alkalis, the sulfates and the chlorides in the gas condense on the cooler surfaces, the condensation temperatures are in the range of 600 to 1000 degrees Celsius for the alkali sulfates, and the condensates are the sticky layers that capture the dust and cement the deposits. The condensation is strongest at the cool wall regions, the uninsulated sections, the flanges and the cold spots, and the condensation products are the alkali sulfates, the chlorides and the sulfates, which are the same salts that form the kiln rings and the preheater deposits. The condensation is the mechanism that transforms the loose dust deposits into the hard, cemented deposits, and the hard deposits are the deposits that the flow cannot remove and that require the mechanical cleaning.

The adhesion is the sticking of the dust to the wall and to the existing deposits: the adhesion depends on the particle properties, the moisture, the temperature and the wall conditions, the fine particles adhere more strongly than the coarse particles, the moist and the sticky particles adhere strongly, and the rough and the coated walls promote the adhesion. The adhesion completes the accumulation cycle: the dust deposits, the deposits provide the surface for the further adhesion, and the deposits grow until they are removed or until they block the duct. The mechanisms are summarized in the reference table below, which is used for the diagnosis of the deposit types:

Mechanism Deposit location Deposit character Main cause Primary remedy
Inertial deposition Bends, dampers, transitions, obstructions Local, dense, growing Coarse dust, flow disturbances, high dust load Flow design, velocity, dampers, cleaning
Turbulent deposition Duct walls, lengthwise Uniform, loose layer Fine dust, low velocity, long horizontal runs Velocity increase, insulation, cleaning
Condensation Cool wall regions, flanges, cold spots Sticky, hard, cemented Alkali and sulfate vapors, cool surfaces Insulation, temperature management, chemistry
Adhesion On existing deposits Layered, growing Sticky dust, rough walls, moisture Surface treatment, cleaning, moisture control

The Causes of the Dust Accumulation

The dust accumulation is caused by the combination of the process, the operation and the design factors, and the identification of the dominant causes is the condition of the effective solution. The main causes are the high dust load of the tertiary air, the low gas velocities, the duct routing, the temperature conditions, the chemistry of the dust and the gas, and the operation of the cooler and the kiln system.

The dust load of the tertiary air is the material input of the accumulation: the tertiary air carries the dust from the cooler, and the dust load depends on the cooler operation, the grate loading, the air distribution and the clinker characteristics. The high dust load is the result of the overloaded cooler, the high grate speed, the poor clinker bed condition, the excess air and the cooler disturbances, and the high dust load accelerates the accumulation by all the mechanisms. The dust load is measured by the sampling and the dust concentration measurements, and the dust load reduction is the first lever of the prevention: the cooler optimization, the air distribution and the clinker condition management reduce the dust carried to the tertiary air duct.

The gas velocity in the duct is the transport capability: the velocity below the design range allows the dust to settle and the deposits to grow, and the low velocity is the result of the oversized duct, the reduced air flow, the damper position and the process changes. The velocity is restored by the air flow management, the damper adjustment and the duct modifications, and the velocity monitoring, the flow measurements and the pressure drop monitoring, is the detection of the velocity problems. The duct routing and the geometry are the structural causes: the long horizontal runs, the sharp bends, the transitions and the obstructions are the locations of the deposition, and the routing is the design constraint of the existing plants, addressed by the retrofit measures.

The temperature conditions are the factor of the condensation and the adhesion: the duct wall temperatures below the condensation temperatures of the volatile salts cause the condensation, the cold spots, the uninsulated sections and the flanges are the condensation sites, and the temperature management, the insulation and the hot spots control, is the prevention of the condensation. The chemistry of the dust and the gas is the factor of the deposit hardness: the high alkali and the sulfur contents of the raw material and the fuel increase the condensation potential, the high chloride contents form the sticky deposits, and the chemistry is managed by the raw mix and the fuel selection and the bypass operation. The operation of the kiln system is the factor of the stability: the unstable operation, the temperature fluctuations, the fuel changes and the cooler disturbances create the conditions of the deposition, and the stable operation is the prevention.

The causes are diagnosed with the evidence: the deposit samples are analyzed for the composition, the dust load is measured, the velocities and the temperatures are measured along the duct, the operating data is reviewed, and the dominant causes are confirmed. The diagnosis is the input of the solution design, and the professional practice is the evidence-based diagnosis, which the article emphasizes throughout.

The Symptoms and the Detection of the Dust Accumulation

The dust accumulation is detected by the symptoms in the operation and by the direct measurements, and the early detection is the condition of the early response: the deposits that are detected early are removed easily, and the deposits that grow undetected cause the production losses and the stops. The main symptoms of the accumulation are the pressure drop increase, the air flow reduction, the temperature changes, the calciner operation changes, the fan load changes and the visible observations.

The pressure drop across the duct is the primary symptom: the deposits narrow the cross-section, the velocity increases through the restriction and the pressure drop rises, and the pressure drop trend is the early indicator of the accumulation. The pressure drop is measured across the duct sections, the baseline is established, and the alarm limits are configured, and the rising pressure drop triggers the investigation and the cleaning. The air flow reduction is the consequence of the restriction: the reduced cross-section reduces the tertiary air flow at the constant fan duty, the calciner receives less air, the combustion conditions change and the calcination is disturbed, and the air flow reduction is detected by the flow measurements and the damper positions.

The temperature changes are the symptoms of the flow and the deposit changes: the deposits reduce the heat transfer at the deposit locations, the duct surface temperatures at the deposits are lower than the surroundings, the reduced air flow changes the temperature profile of the calciner and the kiln, and the temperature monitoring, the surface temperature measurements and the infrared scanning, detect the deposits and the flow changes. The calciner operation changes are the process symptoms: the calciner temperature falls or fluctuates with the reduced air, the fuel must be increased to maintain the temperature, the NOx and the CO change, and the calcination degree falls, which affects the kiln operation and the clinker quality. The fan load changes are the symptoms of the system resistance: the reduced duct cross-section increases the system resistance, the fans move to the higher duties or the lower flows, and the fan power and the flow changes are monitored.

The visible observations complete the detection: the duct sections with the access openings are inspected, the deposit thickness is measured with the probes, the deposit samples are taken for the analysis, and the inspections at the stops record the deposit distribution along the duct. The detection program combines the continuous monitoring, the pressure drop, the flow and the temperatures, with the periodic inspections and the campaigns, and the detection data is the input of the deposit management: the detection, the diagnosis, the prevention and the cleaning.

The Consequences of the Dust Accumulation

The dust accumulation is not only the duct problem: it propagates through the kiln system with the significant consequences for the operation, the efficiency and the availability. The consequences are the reduced production, the increased heat consumption, the disturbed combustion, the equipment damage, the safety issues and the increased maintenance.

The reduced production is the first consequence: the restricted tertiary air flow limits the calciner combustion, the calcination falls, the kiln system is the bottleneck, and the production is reduced below the design, with the production loss quantified by the rate reduction and the duration. The increased heat consumption is the second consequence: the disturbed combustion and the reduced calcination increase the specific heat consumption, the calciner fuel must be increased or the kiln operation is disturbed, and the heat loss is quantified in the fuel cost. The disturbed combustion is the third consequence: the reduced and the unbalanced air flows change the flame, the temperatures and the gas composition, the NOx and the CO increase, the clinker quality is disturbed, and the combustion disturbances propagate to the kiln and the preheater.

The equipment damage is the fourth consequence: the deposits at the dampers damage the damper seats and the actuators, the deposits at the transitions disturb the flow and the erosion of the duct walls increases at the deposits, and the blocked duct forces the kiln system stop, with the stop costs of the lost production and the repair. The safety issues are the fifth consequence: the blocked duct and the disturbed combustion create the risks of the gas leaks, the hot spots and the process upsets, and the cleaning of the deposits is the hot and the dusty work with the safety requirements. The increased maintenance is the sixth consequence: the cleaning campaigns, the damper repairs, the duct repairs and the extended stops are the maintenance costs, and the maintenance workload increases with the accumulation problem.

The consequences are quantified in the economic terms: the production loss, the heat loss, the maintenance costs and the stop costs are the total cost of the dust accumulation, and the quantification is the business case of the prevention and the solution investments. The professional plant quantifies the consequence costs, and the solution decisions, the design changes, the equipment and the operational changes, are based on the quantified business case.

The Prevention of the Dust Accumulation by the Design

The prevention of the dust accumulation starts at the design stage, and the design measures are the most effective and the most economical: the velocity design, the routing, the damper design, the insulation, the cleaning provisions and the monitoring provisions are the design variables that prevent the accumulation from the start.

The velocity design is the first design measure: the duct is sized for the velocity that carries the dust, the design velocity is in the range of 15 to 25 meters per second, the velocity is verified for the operating range, the minimum load conditions and the future conditions, and the oversizing that reduces the velocity is avoided. The routing design is the second measure: the horizontal runs are minimized, the inclined and the vertical sections are preferred, the bends are designed with the large radii, the transitions are gradual, and the obstructions and the sudden changes are avoided. The damper design is the third measure: the dampers are located and oriented to minimize the deposition, the damper seats are protected, and the damper operation, the position and the maintenance, is designed for the dusty conditions.

The insulation design is the fourth measure: the duct is insulated and lined to maintain the gas temperature, to prevent the condensation and to protect the steel, and the insulation design includes the cold spot elimination, the flanges and the supports, and the hot spots management. The cleaning provisions are the fifth measure: the access openings are provided at the deposition-prone locations, the bends, the dampers and the transitions, the cleaning devices, the air cannons and the mechanical openings, are provided, and the cleaning is designed as the planned activity. The monitoring provisions are the sixth measure: the pressure drop taps, the flow measurements, the temperature measurements and the inspection points are provided, and the monitoring data is connected to the control system with the alarms.

The design measures are the domain of the new plants and the major modifications, and the design practice is supported by the flow modeling: the computational fluid dynamics analysis simulates the flow, the dust trajectories and the deposition, and the modeling optimizes the duct design before the construction. The design practice is also the continuous improvement: the operating plants feed the accumulation experience back into the design standards, and the design standards evolve with the experience.

The Prevention of the Dust Accumulation by the Operation

The operation is the second line of the prevention: the operational measures reduce the dust load, maintain the velocities, manage the temperatures and keep the system stable, and the operational prevention is the daily practice of the operators and the engineers. The operational measures include the cooler optimization, the air management, the temperature management, the chemistry management and the stability management.

The cooler optimization reduces the dust load of the tertiary air: the cooler is operated with the correct grate loading, the air distribution is balanced, the clinker bed condition is maintained, and the excess air and the disturbances are avoided, and the cooler optimization reduces the dust carried to the tertiary air duct. The air management maintains the duct velocities: the tertiary air flow is monitored and maintained, the dampers are positioned correctly, the air distribution between the kiln, the calciner and the cooler is balanced, and the velocity is verified with the flow measurements. The temperature management prevents the condensation: the duct temperatures are maintained above the condensation temperatures, the insulation is maintained, the cold spots are eliminated, and the temperature monitoring detects the cold sections.

The chemistry management reduces the condensation potential: the raw mix and the fuel alkalis and the sulfurs are monitored and managed, the sulfur-to-alkali ratio is controlled, the bypass is operated when required, and the deposit samples are analyzed to confirm the chemistry. The stability management prevents the deposition episodes: the kiln system is operated stably, the feed, the fuel and the temperatures are stable, the cooler is stable, and the disturbances are managed with the procedures, because the unstable operation is the time of the deposition.

The operational prevention is supported by the operating procedures: the procedures define the monitoring, the alarm responses, the cleaning triggers and the responsibilities, and the procedures are the documented practice that the operators execute. The operational prevention is verified by the deposit monitoring: the pressure drop, the temperatures and the inspections are reviewed, the accumulation trend is tracked, and the prevention measures are adjusted on the evidence, which closes the operational prevention loop.

The Cleaning of the Dust Accumulation

When the deposits form despite the prevention, the cleaning is the response, and the cleaning methods are selected by the deposit type, the deposit location, the duct configuration and the operating mode. The cleaning methods include the flow-based cleaning, the mechanical cleaning, the pneumatic cleaning and the process cleaning, and the cleaning is performed during the operation where possible and at the stops where required.

The flow-based cleaning uses the air flow itself: the velocity is temporarily increased, the damper is stroked, the flow is pulsed, and the deposits that are loose are entrained and carried out. The flow-based cleaning is the simplest method, effective for the loose deposits, and it is performed by the defined flow procedures, with the monitoring of the pressure drop and the process conditions. The pneumatic cleaning uses the compressed air: the air cannons and the air lances deliver the air pulses and the jets to the deposit locations, the air pulses dislodge the deposits, and the cleaning is performed through the access openings or the installed devices. The pneumatic cleaning is effective for the local deposits, and the air cannons are installed at the deposition-prone locations for the remote cleaning during the operation.

The mechanical cleaning uses the physical contact: the probes, the rakes and the scrapers are introduced through the access openings, the deposits are broken and removed, and the mechanical cleaning is performed during the operation where the access allows and at the stops with the full access. The mechanical cleaning of the hard, cemented deposits is the most labor-intensive method, and it is performed with the safety procedures, the hot work and the confined space precautions. The process cleaning uses the process conditions: the temperature is raised to soften or to shed the deposits, the chemistry is changed to reduce the adhesion, and the operation is adjusted to remove the deposits, and the process cleaning is the combination of the flow, the temperature and the chemistry management.

The cleaning is managed with the cleaning plan: the deposit monitoring identifies the cleaning triggers, the cleaning methods are defined for the deposit types and the locations, the cleaning is scheduled in the operation and the stops, and the cleaning results are verified with the pressure drop and the flow measurements. The cleaning plan is the operational document, and the professional plant plans the cleaning as the routine activity, which prevents the escalation of the deposits to the production losses and the stops.

The Engineering Solutions for the Existing Plants

The existing plants with the recurring dust accumulation apply the engineering solutions, the retrofits that modify the duct and the system to solve the problem. The retrofit solutions are designed on the evidence of the diagnosis, and they are prioritized by the cost-effectiveness and the production impact. The main retrofit measures are the flow modifications, the velocity restoration, the damper modifications, the insulation improvements, the cleaning installations and the system integration.

The flow modifications change the duct geometry: the horizontal sections are converted or modified, the bends are re-profiled with the larger radii, the transitions are modified, and the deposition locations are eliminated or improved. The velocity restoration restores the carrying velocity: the duct is modified to the correct cross-section, the flow is re-distributed, the air management is improved, and the velocity is verified by the measurements. The damper modifications improve the damper behavior: the dampers are replaced or relocated, the damper seats are protected, and the damper cleaning is provided. The insulation improvements eliminate the cold spots: the insulation is completed and improved, the flanges and the supports are insulated, and the condensation is prevented. The cleaning installations provide the cleaning capability: the air cannons are installed at the deposition-prone locations, the access openings are provided, and the cleaning devices are installed. The system integration addresses the upstream causes: the cooler is modified or optimized to reduce the dust load, the air distribution is improved, and the chemistry is managed by the bypass or the raw mix changes.

The retrofit solutions are implemented with the engineering process: the diagnosis, the solution design, the cost-benefit analysis, the implementation and the verification. The implementation is performed at the planned stops, with the design, the fabrication and the installation quality controlled, and the verification measures the pressure drop, the flow and the temperatures after the retrofit, confirming the solution effectiveness. The retrofit projects are the professional engineering work, and the project documentation, the design, the drawings and the reports, is the knowledge base of the plant.

The Monitoring and the Management Program

The tertiary air duct dust accumulation is managed with the continuous program: the monitoring, the diagnosis, the prevention, the cleaning and the improvement, and the program is the institutionalization of the practice. The monitoring program includes the pressure drop, the flows, the temperatures, the inspections and the deposit sampling, with the defined frequencies and the alarm limits. The diagnosis program includes the deposit analysis, the cause analysis and the solution development, with the documentation and the review. The prevention program includes the design and the operational measures, the procedures and the training, and the cleaning program includes the cleaning plan, the methods and the verification. The improvement program includes the retrofit projects, the design standards and the experience transfer, and the program is reviewed periodically with the performance data.

The program data includes the deposit events, the cleaning campaigns, the pressure drop and the flow trends, the production and the heat data, and the costs, and the data is the evidence of the program effectiveness. The program reviews compare the accumulation frequency, the production impact and the costs with the targets, and the reviews identify the remaining gaps and the improvement actions. The program is the management system of the problem, and the professional plant manages the dust accumulation like the other major risks of the kiln system, with the data, the analysis, the actions and the reviews.

The program is completed by the knowledge and the training: the operators and the engineers understand the mechanisms, the causes, the detection, the prevention and the cleaning, the training is delivered on the procedures and the practice, and the experience is transferred through the documentation and the handover. The knowledge is the foundation of the program, and the professional plant invests in the knowledge as well as in the equipment, which is the practice that keeps the tertiary air ducts of the kiln systems clean, the combustion stable and the production at the design, which is the outcome that this article is designed to support.

Frequently Asked Questions

Why does the dust accumulate in the tertiary air duct?

Because the tertiary air carries the dust from the cooler, and the dust deposits by the inertial and the turbulent mechanisms at the bends, the dampers and the low-velocity sections, with the condensation and the adhesion cementing the deposits into the hard layers.

What is the typical velocity of the tertiary air in the duct?

The design velocity is typically 15 to 25 meters per second, high enough to carry the dust and to prevent the deposition, and the velocity below the design range is one of the main causes of the accumulation.

What are the first symptoms of the dust accumulation?

The rising pressure drop across the duct, the reduced tertiary air flow, the temperature changes at the deposit locations and in the calciner, and the disturbed calciner operation, with the pressure drop trend as the earliest indicator.

How are the hard, cemented deposits removed?

The hard deposits require the mechanical cleaning with the probes, the rakes and the scrapers through the access openings, at the stops or during the operation where the access allows, together with the address of the condensation causes that cemented the deposits.

Can the dust accumulation be prevented by the design?

Yes, the design prevention includes the correct velocity, the routing with the minimal horizontal runs and the large-radius bends, the damper design, the insulation, the cleaning provisions and the monitoring provisions, and the CFD analysis supports the design.

What are the consequences of the blocked tertiary air duct?

The reduced production, the increased heat consumption, the disturbed combustion, the higher NOx and the CO, the equipment damage, the safety risks and the forced stops, with the total costs quantified for the solution business case.

Summary and Final Recommendations

This article has addressed the tertiary air duct dust accumulation problem in the professional depth: the function and the design of the duct, the mechanisms of the accumulation, the causes, the symptoms and the detection, the consequences, the prevention by the design and the operation, the cleaning methods, the engineering solutions for the existing plants and the monitoring and the management program. The article has provided the reference table of the accumulation mechanisms and the complete toolbox of the diagnosis, the prevention and the solution, in the generic form that applies to any kiln system. The recommendations for the plant facing this problem are these: diagnose the evidence, the deposit samples, the dust load, the velocities, the temperatures and the operating data, because the effective solution follows the confirmed causes; prevent by the operation, the cooler optimization, the air management, the temperature and the chemistry management and the stability, because the operational prevention is the daily practice; monitor the trends, the pressure drop, the flows and the temperatures, with the alarms, because the early detection is the early response; clean systematically, with the defined methods, the triggers and the verification, because the planned cleaning prevents the escalation; and engineer the solution, the retrofits that restore the velocity, improve the routing, eliminate the cold spots and reduce the dust load, because the engineering solution is the lasting solution. The tertiary air duct is the artery of the precalciner system, and the dust accumulation is the disease of the artery, and the professional understanding and the practice that this article provides keep the artery open, the combustion stable and the kiln system at the design performance, which is the outcome that every plant with a precalciner requires.

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