Prisma ODS Revista Científica Multidisciplinar

Volumen 5, Número 5 - Año 2026

Página | 1

PORTADA

(Elaborada por la revista)

Prisma ODS Revista Científica Multidisciplinar

Volumen 5, Número 5 - Año 2026

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Application of the 8D Methodology to Reduce Failures in the Dust

Filtration System in the Cement Industry

Aplicación de la Metodología 8D para Reducir Fallos en el Sistema de

Filtración de Polvo en la Industria del Cemento

Guillen Barrera Trejo

ba464142@uaeh.edu.mx

https://orcid.org/0009-0008-9227-7731

Universidad Autónoma del Estado de Hidalgo

Hidalgo – México

Karla Yareli Aguilar Diaz

ag381646@uaeh.edu.mx

https://orcid.org/0009-0004-3677-7070

Universidad Autónoma del Estado de Hidalgo

Hidalgo – México

Erick Uriel Morales Cruz

erick_morales@uaeh.edu.mx

https://orcid.org/0009-0008-2071-9713

Universidad Autónoma del Estado de Hidalgo

Hidalgo – México

Luis Ricardo Martínez Pacheco

luis_pacheco5559@uaeh.edu.mx

https://orcid.org/0009-0002-1586-4648

Universidad Autónoma del Estado de Hidalgo

Hidalgo – México

Estella María Esparza Zúñiga

estella_esparza@uaeh.edu.mx

https://orcid.org/0009-0008-2603-1311

Universidad Autónoma del Estado de Hidalgo

Hidalgo – México

Artículo recibido: 01/09/2026

Aceptado para publicación: 09/10/2026

Conflictos de Intereses: Ninguno que declarar

Autora de correspondencia.

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ABSTRACT

In the present investigation, the 8D methodology was used to solve a problem of filter

bag breakage in a complex dust collection system caused mainly by premature wear of the

filters, this generated inefficiency in both the operating process due to material losses causing

environmental damage when particles leak out of the system. In addition to this, it is a

fundamental quality requirement to maintain a controlled process with a purity level > 99%.

The application of the tool showed that due to the complexity of the problem it was necessary

to integrate a broad methodology that included a multidisciplinary group of experts,

determining 3 root causes; improper basket design, poor filter media quality, and improper

operation of the cleaning system. Derived from the main findings, a future control and

prevention plan was designed.

Keywords: ishikawa, 8D methodology, quality, dust collector, filters

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Resumen

En la presente investigación se empleó la metodología 8D para resolver un problema

de rotura de las bolsas filtrantes en un sistema complejo de colección de polvos provocado

principalmente por el desgaste prematuro de los filtros, esto generó ineficiencia tanto en el

proceso operativo debido a las pérdidas de material provocando daños ambientales al momento

de fugarse partículas al exterior del sistema. Aunado a eso es requisito fundamental de calidad

mantener un proceso controlado y con un nivel de pureza > 99%. La aplicación de la

herramienta mostró que debido a la complejidad del problema era necesario integrar una

metodología amplia que incluyera a un grupo multidisciplinario de expertos, determinando 3

causas raíz; diseño inadecuado de la canastilla, calidad deficiente del medio filtrante y

operación incorrecta del sistema de limpieza. Derivado de los principales hallazgos se diseñó

un plan de control y prevención a futuro.

Palabras clave: ishikawa, metodología 8D, calidad, colector de polvos, filtros

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INTRODUCTION

The cement industry currently faces significant production-related challenges due to rising

demand in recent years; according to Moralez Zambrano (2022), cement production in Mexico

will increase in 2020, driven by the construction sector's response to government social

programs. Cement is considered one of the most widely used materials globally, as it is

essential for infrastructure development in the construction of housing, buildings, roads, and

bridges (Arena, Correa & de Rosa, 2002).

Due to its rapid growth, this industry has faced significant challenges in both operational and

environmental areas. The production of this material involves crushing, calcination, and

grinding processes that generate large quantities of dust; consequently, it is essential to have

an adequate filtration system capable of capturing these particles to reintroduce them into the

process rather than releasing them into the environment. Among the most widely used filtration

systems are filter bags, which consist of a synthetic fiber filtering surface designed to retain

particulate matter (Díaz & Velázquez, 2019) and a metal structure, known as a cage and located

inside the bag, that provides rigidity and prevents deformation (Sosa, 2022).

Filter bags operate via a system in which a dust-laden air stream enters and passes through the

bags; dust particles are trapped on the bag walls, while clean air exits the system. Periodically,

a burst of compressed air is released, dislodging the trapped dust and causing it to fall into a

hopper located at the bottom of the filtration system (Rivera, 2019). This entire process enables

the recovery and reintroduction of a significant portion of the material, thereby reducing the

waste generated.

Filtration systems are constantly subjected to extreme operating conditions, including high

temperatures and continuous contact with abrasive particles generated during the process.

These factors directly affect the equipment's durability, and consequently, various problems

often arise that prevent the system from functioning correctly. Among the most common

problems are filter saturation, filter bag rupture, excessive cleaning, cage deterioration,

abrasion, and corrosion. Of the numerous possible failures, filter bag rupture plays a critical

role in system performance: ruptures allow particles to escape into the environment, resulting

in the loss of material that should have been recovered.

Filter bag rupture is considered a critical failure in the cement industry due to the associated

environmental and production complications; therefore, a detailed analysis of the multiple

potential causes of this issue is required. In this article, we employ the Eight Disciplines (8D)

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problem-solving methodology, which is designed to address problems of unknown origin with

the aim of process improvement (Kaplík, Prístavka, Bujna & Viderňan, 2013), by following a

sequential process until the issue is resolved through the implementation of a permanent

solution (Barosani, Bhalwankar, Deshmukh, Kokane & Kulkarni, 2017). Beyond addressing

the specific problem at hand, this approach prevents the emergence of further complications

resulting from the system failure (Rathi, Reddy, Narayana, Narayana & Rahman, 2022).

Against this backdrop, this article analyzes filter bag rupture failures in the cement industry

using the 8D methodology, aiming to identify the root cause of the issue and devise an optimal

solution that eliminates the problem at its source.

METHODOLOGY

This study focused on a dust collection system serving the calcination process in the cement

industry. During system operation, premature failures were observed in the collector's filter

bags; specifically, tears appeared at the top of the bag (the collar), allowing a portion of the

generated emissions to escape into the atmosphere. This reduced the capture system's

efficiency and necessitated unscheduled shutdowns to replace the damaged filter bags. To

identify the root causes of the problem, the 8D (Problem-Solving Process) methodology was

employed. By assembling a competent, multidisciplinary team and following a structured

analysis process, utilizing various quality tools and sound decision-making, we were able to

resolve the issue.

Table 1. 8D methodology

8D METHODOLOGY

Problem assessment.

Team formation.

Problem description.

Containment actions.

Root cause identification.

Permanent corrective actions.

Implementation of corrective actions.

Prevention of recurrence.

Closure and recognition.

Source: own elaboration.

D0: Here, a problem directly impacting the company is identified, and the severity of the

situation is assessed to determine whether this methodology needs to be applied.

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D1: In this stage, a team is assembled possessing knowledge and skills related to the process

or product, specifically the area under review and those affected by the problem. Team

members must have the authority to implement changes and the capacity to provide responses

that drive improvement. It is necessary to assign roles to each team member and clearly define

their responsibilities.

D2: Data collection takes place, presenting specific and historical information. A clear and

precise explanation is provided regarding what is happening, where the failure occurs, the

number of defective parts, who performs the operation, and when and how the problem

occurred, all without yet addressing the root cause of the problem.

D3: An emergency response is created by implementing interim measures to ensure the

customer is not affected while a definitive solution is reached.

D4: Quality tools such as the Ishikawa diagram, the "5 Whys," or the Pareto chart are used here

to rule out potential causes of the failure and identify the root cause of the problem.

D5: The root cause is analyzed to determine and select the best possible solution. It is essential

to ensure that the corrective actions permanently resolve the root cause of the problem.

D6: Permanent corrective actions are implemented based on a plan; it is important to verify

that the actions taken are effective in resolving the problem. The containment action should be

eliminated once it is confirmed that the corrective actions are functioning properly.

D7: Now that actions have been taken to fix the failure, the system, processes, or procedures

are analyzed to prevent the failure from recurring in the future, thereby avoiding a repeat of the

same problem.

D8: Upon completion of the 8D’s process, the results are documented, and the efforts of the

individuals involved in resolving the issue are recognized; this motivates team members to

participate in future situations that may arise.

Case study

The study was conducted at the facilities of a cement manufacturing company; its operations

range from the extraction and processing of raw materials such as limestone, clay, and other

minerals to their transformation into cement through industrial processes.

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D0: Problem Assessment: The production process utilizes various dust filtration systems to

ensure the reincorporation of collected material and compliance with environmental

regulations. In recent weeks, recurring atmospheric emissions have been detected from one of

the main filters, compromising operational efficiency and causing unscheduled shutdowns.

D1: Team Formation: A multidisciplinary team was assembled to gather information for

analyzing and resolving the problem. The company's General Manager serves as the team

leader, and the team is composed of the following members:

Table 2. Work team

PLANT MANAGER

Provides the necessary resources for the investigation and

approves corrective actions involving investments or

modifications to the filtration system.

PRODUCTION

MANAGER

Responsible for providing information regarding the

collector's operating conditions.

MAINTENANCE

MANAGER

Coordinates all technical activities related to the inspection

and repair of the filtration system.

FILTRATION

SPECIALISTS

Provide expertise on the operation of collectors and filter

elements. They analyze the physical condition of the bags,

cages, and cleaning system, as well as the collector's

operating conditions.

MAINTENANCE

ASSISTANTS

Perform tasks such as removing filter bags, replacing

damaged elements, and assisting in the implementation of

corrective actions.

Source: own elaboration.

D2. Problem description: As shown in Table 3, the emissions resulted from damage to various

bags. During April and May 2026 a period spanning eight weeks inspections of the collector

were conducted to assess the impact of the failure and replace the damaged bags.

Table 3. Percentage of damaged bags

WEEK

BAGS

Total

4,620

Defects

0.54

0.74

0.43

0.52

0.63

0.45

0.32

0.74

Source: own elaboration.

Based on this data collection, it can be observed that, on average, 0.55% of the bags rupture

due to various causes. Although 0.55% may seem low, this percentage of ruptured bags

represents an increase in emissions resulting from the direct passage of unfiltered dust.

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Inspections of the various compartments reveal that the primary bag failure occurs in the upper

section, as shown in Figure 1.

Figure 1.Breakage of upper part 1.

Source: own elaboration.

Figure 2. Ruptured bags

Source: own elaboration.

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Figure 3. Breakage of upper part 2

Source: own elaboration.

Figure 4. Upper part breakage 3

Source: own elaboration.

Currently, the company operates its cleaning system on a continuous basis, that is, over a fixed

time interval, involving set cleaning cycles and discharge pressures. This system is very simple;

it operates for a predetermined duration regardless of the actual cleanliness of the bags. This

results in inefficient cleaning, as the system continues to discharge compressed air

unnecessarily, wasting electricity even when the plant generates less dust during a shift.

Table 4. Continuous cleaning cycles

CYCL

ΔP

CYC

ΔP

CYC

ΔP

CYCL

ΔP

5.53

7.64

4.17

6.85

5.24

3.14

4.28

5.79

3.04

3.52

5.57

6.41

7.43

5.61

7.05

5.07

2.80

7.81

6.79

4.75

4.40

2.18

6.77

2.31

5.98

4.06

3.18

5.45

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5.84

4.43

6.50

3.96

Note: *ΔP = Pressure differential.

Source: own elaboration.

The manufacturer establishes a critical operating limit of 6 inH2O, as a high pressure

differential results in increased energy consumption; the exhaust fan must work harder to move

the same volume of air. For this reason, specialists recommend configuring the cleaning system

based on pressure differential rather than time, setting upper and lower limit values. Graph 1

illustrates these limits as well as the measurements from Table 4.

* inH2O = Inches of water column; measures the pressure exerted by a column of water one

inch high.

Graph 1. Pressure difference limits

Note: LS: Upper limit, 6 in H2O. LI: Lower limit, 2.4 in H2O. LC: Center limit, 4.4 in H2O.

ΔP: Pressure differential, current ranges.

Source: own elaboration.

As shown in Graph 1, the cleaning cycles run continuously, causing the bags to undergo

cleaning even when not required. In instances of higher dust loads, filter pressure rises;

consequently, the company decided to increase the pulse pressure from 4 bar to 6 bar.

D3: Containment actions. Based on the observed differential pressure behavior, it is

recommended to switch from time-based cleaning cycles to differential pressure (ΔP) based

cycles. This will prevent unnecessary cleaning cycles; the cycle will initiate when the

differential pressure reaches 6 inH2O and stop at 4 inH2O, thereby mitigating the fatigue bags

experienced during each cycle due to compression and tension stresses. Additionally, the pulse

pressure should be reduced from 6 bar to 3 bar, as higher cleaning pressures increase fatigue

stress, leading to premature bag damage.

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D4: Root cause identification. To understand the root cause of the problem, the team has

decided to use analysis tools such as the Ishikawa diagram; this will enable the team to identify

the various factors contributing to the issue.

Figure 2. Ishikawa diagram for the analysis of causes of filter bag failure

Source: own elaboration.

Labor: It was found that the filter bags in the filtration system were improperly installed due

to inadequate staff training; furthermore, the inspections being conducted were deficient.

Machine: The cages installed in the filtration system are poorly designed, as they lack a venturi

to accelerate fluid flow; consequently, the air does not move at the proper speed to traverse the

entire bag. This results in uneven cleaning, as the bag is too large. Additionally, the connection

between the collar and the cage's vertical ribs is exposed and in direct contact with the bag,

causing weld defects to tear the bag at the top, as shown in Figure 3.

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Figure 5. Bag torn at the neck

Source: own elaboration.

Figure 6. Welding defect.

Source: own elaboration.

Material: A bag was sampled for laboratory analysis, yielding the following results.

Microscope images reveal the deterioration of the PTFE membrane and dust accumulation

within the fabric structure, leading to saturation, as shown in Figure 4.

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Figure 7. Surface of the bag

Source: own elaboration.

Figure 8. Dust penetration

Source: own elaboration.

As shown in Table 5, the mass per unit area indicates significant particle accumulation and dust

impregnation within the fiber structure as can be seen in Figure 5 since the cleaning process

failed to restore the nominal value. Regarding air permeability, the results fall within the

reference range; however, these values are very low compared to the quality of other filter

fibers. Permeability doubles after cleaning; this fact, combined with the visual inspection,

confirms the observed deterioration of the membrane.

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Table 5. Weight control and air permeability

SECTION

WEIGHT (G/M²)

PERMEABILITY (L/DM²/MIN)

MEASURED

REFERENCE

SUPERIOR

LOWER

REFERENCE

As received

873.33

770

13.59

14.05

9 - 30

After

cleaning

854.66

29.74

36.03

Note: *The reference values are taken from the bag manufacturer's technical data sheet.

Source: own elaboration.

The rupture test values presented in Table 6 demonstrate a significant decline in the mechanical

properties of the bags compared to the reference values; this indicates that the bags are already

substandard and compromises system performance due to premature ruptures.

Table 6. Breaking load and elongation at break

SECTION

BREAKING LOAD (DAN/5CM)

ELONGATION AT BREAK (%)

SUPERIO

LOWE

REFERENC

SUPERIO

LOWE

REFERENC

Longitudin

234.95

220.85

Length: ≥

400

Width: ≥ 300

10.88

10.39

—

Cross

286.92

201.97

4.38

5.88

Note:*The reference values are taken from the bag manufacturer's technical data sheet.

Source: own elaboration.

Based on the results obtained during the visual inspection and laboratory tests, it is concluded

that the fiberglass filter bag exhibits a level of deterioration that compromises its performance.

Laboratory test methods for filter fabrics

Air permeability: [In accordance with standard SFS-EN ISO 9237]: The airflow rate passing

perpendicularly through a specific area of the fabric is measured at a specific pressure

difference across the test area over a set period of time.

Equipment: Air permeability tester.

Test area: 20 cm²

Pressure drop: 200 Pa

Area density (weight per unit area): [In accordance with standard SFS-EN 12127]: The mass

of a known area of the fabric is divided by that area, expressed in grams per square meter.

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Equipment: Precision balance, accuracy ± 3 mg.

Test result: Mean mass per unit area, in grams per square meter.

Tenacidad de rotura y alargamiento de rotura: [De acuerdo a la norma SFS-EN ISO 13934-1]

Breaking tenacity and elongation at break: [In accordance with standard SFS-EN ISO 13934-

Method: A test specimen of specific dimensions is subjected to extension at a constant speed

until rupture. The maximum force and the elongation at the point of maximum force are

recorded.

Equipment: Tensile testing machine for strength and elongation.

Test speed: 300 mm/min

Gauge length: 100 mm

Test results: Arithmetic mean of the maximum force in daN/5 cm in the longitudinal and

transverse directions, as well as the arithmetic mean of the elongation at the point of maximum

force, expressed as a percentage in both directions.

Method: The company establishes its cleaning frequency based on time; this results in the

system being cleaned when not yet required, subjecting the bags to unnecessary stress.

D5: Permanent corrective actions. Based on the results of the root cause analysis, the necessary

corrective actions are established to mitigate and eliminate the fundamental causes of the bag

failures. Replacing the filter medium with a higher-quality one is proposed; this will help

significantly improve the collector's performance.

It is proposed to replace the filter medium with one of higher quality. This will help

significantly improve the collector's performance.

Table 7. Comparison of filter media

CHARACTERISTICS

CURRENT

PROPOSAL

Raw material

100% Fiberglass

Weight

770 g/m2

750 g/m2

Thickness

0.8 - 1.1 mm

0.9 mm

Density

— — —

0.83

Permeability

9 - 30 l/dm2/min

25 - 45 l/dm2/min

Temperature resistance

260°C continuous flow (dry

heat)

240°C continuous flow (dry

heat)

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Finish

Polytetrafluoroethylene

(PTFE) membrane

Microporous

polytetrafluoroethylene

(PTFE) membrane

Source: own elaboration.

Table 7 shows a decrease in temperature resistance, dropping from 260°C (with the currently

used material) to 240°C (with the proposed material); this poses no risk, as the system's

operating conditions indicate a maximum gas temperature of 220°C, meaning the reduction in

the proposed material's resistance does not affect the system. The new material offers a

significant improvement in filter medium permeability increasing from a range of 9–30

L/dm²/min to 25–45 L/dm²/min which indicates higher airflow through the medium and,

consequently, better filter performance. Furthermore, the incorporation of a microporous PTFE

membrane ensures atmospheric emissions of less than 10 mg/m³.

The cage is a critical component, and a poor design compromises the performance of the filter

medium; therefore, a complete redesign of the cage is proposed.

Figure 6 illustrates the current cage design, which features a short, funnel-style collar and a

junction point where the longitudinal wires connect to the collar; this area remains exposed and

in direct contact with the filter bag seal.

Figure 9. Current design of the basket

Source: own elaboration.

Figure 9 illustrates the new proposed design, which incorporates a three-piece assembly (cage,

straight collar, and venturi). This configuration ensures better distribution during bag cleaning,

thereby improving filter performance; additionally, the straight collar protects the top of the

bag, preventing tears caused by direct contact with weld seams.

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Figure 10. Proposed design

Source: own elaboration.

The fit between the filter bag and the cage is crucial for optimal pulse-jet filter performance. A

filter that is too tight or too loose will result in poor dust collection and is prone to premature

failure. Therefore, parameters exist to determine the ideal fit often referred to as the "pinch"

between the bag and the cage, as shown in Figure 8.

Figure 10. The "pinch" is calculated by subtracting the actual cage circumference from the bag

circumference (flat) and then multiplying the result by Pi divided by 2

Source: Parker Hannifin Corporation (2018).

Table 8 shows the clamping tolerance according to tissue type.

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Table 8. Nominal clamping recommendation

TELA

PINCH

Fieltros

0.25“ - 0.75”

(6.4 - 19 mm)

PPS

0.25” - 0.5”

(6.4 - 12.7 mm)

P84

0.125” - 0.375”

(3.2 - 9.5 mm)

Fibra de Vidrio con membrana de PTFE

0.0” - 0.1875”

(0.0 - 4.8 mm)

Source: Parker Hannifin Corporation (2018).

The previous cage had a diameter of 126 mm, based on the dimensions of the filter bag (which

had a lay-flat width of 200 mm); this ratio resulted in a "pinch" of 4.7 mm. Although this value

fell within acceptable parameters, it was at the upper limit of the permitted range.

Consequently, it was proposed to increase the cage diameter to 128 mm, thereby reducing the

pinch to 0.6 mm. In pulse-jet cleaning filters, bags are subjected to thousands of air pulses

throughout their service life; with each pulse, the bag inflates and, upon completion of the

cleaning cycle, contracts against the cage, generating considerable tension. Reduced pinch

especially with fiberglass bags provides superior mechanical support, which decreases fabric

fatigue and extends service life.

D6: Implementation of corrective actions. The filter bag material was modified: fiberglass bags

with a standard PTFE membrane finish were replaced with bags made of the same base material

but featuring a superior-quality microporous PTFE membrane finish. This change extended the

bags' service life and improved filter efficiency by capturing more particles and optimizing

overall performance. Additionally, cages with a new design were installed; this design allows

for full airflow circulation around the bag, ensuring uniform dust distribution along its entire

length. The redesigned cage features welds on the inner face of the collar, preventing direct

contact with the bag and resolving the issue of premature wear. Furthermore, maintenance

personnel received training on the correct installation of bags and cages to ensure optimal

pinch, thereby minimizing mechanical stress on the bags and extending their durability. Finally,

periodic inspections are conducted to ensure the proper functioning of the entire system.

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Table 9. Percentage of damaged bags after the implemented improvements

WEEKS

BAGS

Total

4,620

Defects

Source: own elaboration.

As shown in Table 9, the implemented improvements resulted in a significant reduction in

premature bag failures; this notably reduced unplanned downtime, increased filtration

efficiency, and simultaneously lowered unforeseen costs.

D7: Prevention of recurrence. As shown in Figure 9, a control plan was established to verify

the proper condition of system components from receipt of materials from suppliers through to

installation and operation in the filtration equipment using direct measurement and visual

inspection as control methods.

Figure 11. Control Plan

Source: own elaboration.

D8: Closure and recognition. Upon completion of the analysis using the 8D methodology, the

problem was resolved favorably for the company. Consequently, team members are recognized

for contributing their ideas, knowledge, and skills to ensure the filtration systems operate with

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the desired efficiency; this achievement was made possible through the effort, perseverance,

and dedication of each individual.

RESULTS AND DISCUSSION

According to Morales (2022), the 8D tool proved highly effective in resolving a customer

complaint regarding a fuel module that failed a flow performance test, thereby eliminating the

root cause of the complaint. This research followed the same steps as the aforementioned

author, with the distinction that the team was multidisciplinary; as in that study, the problem

was eliminated by identifying the root cause and implementing preventive measures.

Similarly, Montiel (2025) found that applying the 8D method led to a 37.48% reduction in total

tool consumption, optimizing operating costs and resource management efficiency, while also

surpassing the benchmark standard established within the Hoshin Kanri framework. Like that

author, this study succeeded in reducing maintenance and operating costs by completely

eradicating the root cause of the problem.

Zamudio (2025) implemented containment actions to prevent the shipment of non-conforming

parts to the customer; these measures ensured operational continuity and maintained customer

satisfaction while the origin of the problem was investigated. Likewise, similar actions were

carried out in the present case, focusing corrective measures on the cleaning system by reducing

the frequency and pressure of discharge pulses. This decreased fatigue on the filter medium,

allowing the system to remain operational while the root cause was identified.

Rosas (2025) applied the 8D methodology at the company Pardalix to identify the root cause

of workplace inefficiencies using analysis tools; The proposed corrective action involved an

ergonomic workstation designed to improve operator performance. The study identified the

filter material and basket design as the primary causes of filtration system failures;

consequently, the filter medium was replaced and the basket redesigned to enhance

performance and extend service life.

Izaguirre (2017) applied Failure Mode and Effects Analysis (FMEA) to prevent failures in

refrigeration equipment, identifying potential issues and establishing preventive actions based

on their criticality. Additionally, this project utilized a control plan to prevent the recurrence of

bag failures by implementing inspection methods and reaction plans that covered everything

from material receipt to actual operations.

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The 8D methodology is widely used across various industrial sectors, as it facilitates problem-

solving through a systemic approach, leading to the proposal of solutions and the prevention

of recurrence. By employing this methodology, Escalona (2024) achieved a 50% reduction in

the consumption of personal protective equipment (PPE) at an automotive company, thereby

optimizing its budget. Similarly, the present study achieved a significant reduction in the use

of filter bags.

CONCLUSIÓN

The application of improvement tools and techniques has proven effective in resolving

complex problems that could not otherwise be solved without a systematic, methodological,

analytical, and engineering-based approach. Among these tools, the 8D methodology has once

again demonstrated that a problem's root cause can stem from multiple factors, highlighting the

advantages and merits of such a comprehensive approach. Furthermore, the constant and

ongoing changes in products, inputs, and technology compel us to adapt and employ

methodologies like 8D in any environment.

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Internacional (CC BY 4.0). Esto permite el uso, distribución y reproducción en cualquier medio, incluidos fines

comerciales, siempre que se otorgue la atribución adecuada a los autores y a la fuente original.

: https://doi.org/10.65011/prismaods.v5.i5.358

Cómo citar este artículo (APA 7ª edición):

Barrera Trejo, G., Aguilar Diaz, K. Y., Morales Cruz, E. U., Martínez Pacheco, L. R., &

Esparza Zúñiga, E. M. (2026). Application of the 8D Methodology to Reduce Failures in the

Dust Filtration System in the Cement Industry. Prisma ODS: Revista Multidisciplinaria Sobre

Desarrollo Sostenible, 5(5), 31-53. https://doi.org/10.65011/prismaods.v5.i5.358

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