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Prepared by: Omid Pourhosseini Professor Fuzhan Nasiri
Availability-based maintenance scheduling in Domestic Hot Water of HVAC system Prepared by: Omid Pourhosseini Professor Fuzhan Nasiri
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What is the main focus in reliability centered maintenance approach?
Decreasing maintenance period in order to limit employing human and financial resources. Reducing the number of maintenance in predefined period to improve availability of the system. Avoiding over maintenance on components with low maintenance effect, and paying more attention to components with high maintenance effect.
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Objective The purpose of this research is to assign an organized maintenance scheduling in Domestic Hot Water of HVAC system in a commercial buildings. The seasonality in this maintenance plan has a significant role. The main focus in this system is on Heat Exchangers as a critical component in terms of cost. Lack of heat exchanger function in the system should be compensated with electrical system, which imposes considerable cost. The purpose of this research therefore is to explore a solution to organize the maintenance plan with dependency on few data.
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Table of content Introduction Literature review Methodology Case study
DHW sub-systems System reliability measurement Sensitivity analysis Availability analysis Replacing the parallel with the standby structure Replacement analysis Conclusion
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Introduction Literature review Methodology Case study Conclusion Introduction The concept of maintenance, be it preventive or corrective, plays a very important role in sectors such as manufacturing, construction, production . It plays a key role in enhancing the efficiency of any system as well as decreasing the possibility of the occurrence of accidents Maintenance can either be preventive or corrective; however, a periodic maintenance provides the possibility of cost efficiency gains by improving the reliability of a system, avoiding failure and preventing defects. Adopting the preventive maintenance approach also has its own disadvantages, which include: Unavailability of sufficient failure data Involvement of many physical parameters Complexity of existing models Difficulty in determining model parameters by using actual data.
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Introduction Literature review Methodology Case study Conclusion Introduction Stremel [1] suggested a probabilistic maintenance scheduling method for organizing system planning Yamayee, Mukherjee [2] [3] considered minimizing production cost as a criterion for maintenance scheduling. Marvn [4] proposed a structured approach to RCM and discussed various steps Selvik and Aven [5] proposed reliability and risk centered methodology(π
π
πΆπ), which is an extension of π
πΆπ
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Introduction Literature review Methodology Case study Conclusion Reliability centered maintenance (π
πΆπ) is a technique to organize preventive maintenance RCM method is analyzed based on twelve consecutive stages as follows [4]: Study preparation System selection and definition Functional failure analysis (FFA) Critical item selection Data collection and analysis FMECA maintenance type selection Determination of maintenance interval Preventive maintenance comparison analysis Treatment of non-critical items Implementation In-service data collection and updating
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Introduction Literature review Methodology Case study Conclusion Definition the reliability is quantified as the probability that a system continues its intended function in different time intervals without repair and maintenance Reliability centered maintenance (RCM) is an analytical technique for scheduling a preventive maintenance (PM) RCM is established to stabilize both cost and benefits in order to achieve an effective preventive maintenance Availability is the ability of a component, which is required to perform expected function in specific time interval Density function is a measure of the overall speed at which failure are occurring.
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Introduction Literature review Methodology Case study Conclusion Definition Generally, a system includes a collection of components, which have their own individual roles, in the system function. Complex systems are disintegrated into sub-systems, components, and sub- components in order to perform reliability analysis. Usual structures are determined based on parallel or series.
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Introduction Literature review Methodology Case study Conclusion In series structure, the whole system fails if any individual component in the system fails. Thus, the system operation relies on the successful working of all components in the system (Eq-1) [6]. π
π π‘ = π
π΄ π‘ Γ π
π΅ π‘ Γ π
πΆ π‘ (Eq-1)[6]
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Introduction Literature review Methodology Case study Conclusion In a system with parallel structure, the system fails whenever all of the components stop functioning; so, the performance of the system is dependent on the functioning of at least one component (Eq-2) [6]. π
π π‘ =1β[1β π
π΄ π‘ ]Γ[1β π
π΅ π‘ ]Γ[1β π
πΆ π‘ ] (Eq-2)[6]
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Availability based method (KSA)
Introduction Literature review Methodology Case study Conclusion Availability based method (KSA) Availability based maintenance method provides maintenance scheduling by considering the outcomes of the maintenance on a system, while keeping availability of the current system (before maintenance). βThe maintenance effect (βπ) refers to the system availability increase due to the increase in components availabilities between the neighboring average maintenance interval typesβ (Eq-3)[16]. Hazard function(π π‘ ) is calculated by regression analysis on the result of failure historic data (bathtub curve). Ξπ π,π,π = π π,π,π β π π,π,π+1 (Eq-3)[16]
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Availability based method (KSA)
Introduction Literature review Methodology Case study Conclusion Availability based method (KSA) The failure density function, the reliability function, and the mean time to failure can be defined based on (Eq-4,5,6) as follow: The availability of a component can be quantified by the mean time to failure(ππππΉ), and the mean time to repair (ππππ
) by Eq-7. π π‘ =π π‘ ππ₯π β 0 π‘ π π ππ (Eq-4)[15] π
π‘ =ππ₯π β 0 π‘ π π ππ (Eq-5)[15] ππππΉ= 0 β π‘Γπ π‘ ππ‘ = 0 β π
π‘ ππ‘ (Eq-6)[15] π π,π,π = ππππΉ MTTF+MTTR (Eq-7)[15]
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Modified failure density function
Introduction Literature review Methodology Case study Conclusion Modified failure density function The failure density function and reliability function must be modified based on the maintenance interval time( π π ). In this approach, π π (π‘) is denoted as the failure density function, π π is the fixed time interval between maintenances and π
(π‘) is the reliability function (Eq-8) [6]. The modified failure density function in the component, after performing maintenance, could be illustrated in Eq-9[6] π
π π π is scaling factor π 1 π‘ = π π π‘ 0<π‘< π π ππ‘βππ€ππ π (Eq-8)[6] π π β π‘ = π=0 β π 1 (π‘βπ π π ) π
π ( π π ) (Eq-9)[6]
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Modified failure density function
Introduction Literature review Methodology Case study Conclusion Modified failure density function the general form of modified failure density function with Weibull distribution, is presented by Eq-10. π π β π‘ as a modified failure density function is dominated by maintenance interval time ( π π ) , and number of maintenance during operation period (πΎ). The modified reliability function, which follows Weibull distribution in general form, is presented by Eq-11. π π β π‘ = π=0 β π½ (π‘βπ π π ) π½β1 πΌ π½ ππ₯π β ( π‘βπ π π πΌ ) π½ π
π ( π π ) (Eq-10) π
π β π‘ = π=0 β ππ₯π β ( π‘βπ π π πΌ ) π½ π
π ( π π ) (Eq-11)
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Modified failure density function
Introduction Literature review Methodology Case study Conclusion Modified failure density function A typical π π β π‘ π
π β π‘ graphs are presented as follows . The time scale is divided into equal time intervals, which is denoted by π π . Generally, Periodic preventive maintenance changes the failure density function from its original shape to exponential form. periodic maintenance in a component causes reduction in failure density function value, and improving time random variable, which prolongs component useful life.
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Modified failure density function
Introduction Literature review Methodology Case study Conclusion Modified failure density function A typical π π β π‘ π
π β π‘ graphs are compared with current failure density function (π(π‘)) and reliability function (π
(π‘)) in the following figures .
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Introduction Literature review Methodology Case study Conclusion Sorting list In the sorting process, component availabilities in each average maintenance interval types are sorted in ascending order based on maintenance effect[16]. components with large maintenance effect (components with major effect in the system availability) are selected to be maintained more frequently [16]. Components with small maintenance effect (components with minor effect in the system availability) are also selected, and the number of maintenance tasks for these components is decreased to prevent over-maintenance in order to reduce maintenance cost [16].
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KSA method (decision process)
Introduction Literature review Methodology Case study Conclusion KSA method (decision process) This flowchart indicates decision process in KSA method.
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KAS method (decision process)
Introduction Literature review Methodology Case study Conclusion KAS method (decision process) The βBottom Loopβ sequences in the KSA decision process are illustrated as follows: the availability ( π΄ π ) for the current system is determined the decision process starts from the βbottom-loopβ. The average maintenance interval type is reduced by one level After calculation of modified availability ( π΄ π β ), it is compared with current system availability ( π΄ π ) If π΄ π β < π΄ π , the βbottom loopβ is adjusted again until it attains at least the current system availability If there is improvement in the system availability, the decision process will move to the βtop-loopβ.
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KAS method (decision process)
Introduction Literature review Methodology Case study Conclusion KAS method (decision process) The βTop Loopβ sequences in the KSA decision process are illustrated as follows: the component from the βtop-loopβ of the ordered list is selected The average maintenance interval type is raised by one level After calculation of modified availability ( π΄ π β ), it is compared with current system availability ( π΄ π ) If π΄ π β β₯ π΄ π , the βtop-loopβ will continue to run. Otherwise, the decision process will be transferred to the βbottom-loopβ This process will continue until the βSTEP Noβ for βbottom loopβ and βtop loopβ are the same KSA approach relies on keeping system availability after maintenance scheduling, while reducing the number of maintenance task .
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Replacement interval (spare parts)
Introduction Literature review Methodology Case study Conclusion Replacement interval (spare parts) This approach relies on replacement, which occurs at a specific time interval (T) along with minimal repair (preventive maintenance) between two consecutive replacements [17]. The expected maintenance cost in each time interval is defined in Eq-12. In this equation, πΆ 1 is the repair cost, πΆ 2 is the replacement cost, and π» π is cumulative hazard function. the result of total expected cost πΈππΆ π , if the component follows Weibull distribution, is determined by Eq-13. πΆ 1 π» π + πΆ 2 (Eq-12)[18] πΈππΆ π = πΆ 1 π π π½ + πΆ 2 + πΆ 1 ππ π ππ 0 π π‘ π½ π βππ‘ ππ‘ π ππ β1 (Eq-13)[18]
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Optimal Replacement period
Introduction Literature review Methodology Case study Conclusion Optimal Replacement period Generally,the optimal replacement interval (T), which satisfies minimal expected total cost, is calculated by Eq-14 [18]. The optimal replacement time ( π β ) is determined by Eq-15,16 [18]. π β is the time replacement interval , πΆ 2 πΆ 1 is the rate of replacement cost to repair cost, and π½ and π are Weibull reliability parameter ππΈππΆ(π) ππ =0 (Eq-14)[18] π β =[ πΆ 2 πΆ 1 π π½β1 ] 1 π½ (Eq-15)[18] π= 1 πΌ π½ (Eq-16)
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Introduction Literature review Methodology Case study Conclusion DHW system of HVAC In this study, maintenance plan in Domestic Hot Water of HVAC system in the commercial building in Canada is taken into account. There is a restriction for HVAC system to be in operation without interruption during the long cold season (the availability of components). HVAC system is categorized as a repairable system. It means that all components are repaired, maintained, adjusted or changed during the life time of the system. In this research, the combination of useful life and wear-out regions in the bathtub curve is taken into account.
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Introduction Literature review Methodology Case study Conclusion DHW sub-systems The Domestic Hot Water system is divided in three main sub-systems as follows: Heating production sub-system (π»π·) Distribution sub-systems in both the utility and process lines (π·π ,π·π) Heat transfer sub-system (π»π)
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Introduction Literature review Methodology Case study Conclusion DHW sub-systems The following P&ID indicates components and the way in which they connect to one another
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Introduction Literature review Methodology Case study Conclusion DHW sub-systems The list of components in each sub-system is presented in the following table. The four mentioned sub-systems have a series arrangement. The reliability analysis in DHW system is illustrated in Eq-17 as follows: Sub-system Component Description HP Pipe, Boiler, Check Valve Heating production DU Pipe, Gate Valve, Check Valve, Pump Distribution system HT Pipe, Gate Valve, Heat Exchanger Heat transferring system DP π
π·π»π π‘ = π
π»π β π
π·π β π
π·π β π
π»π (Eq-17)
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DHW sub-systems Heating production sub-system (Eq-18)
Introduction Literature review Methodology Case study Conclusion DHW sub-systems Heating production sub-system (Eq-18) Heat transfer sub-system (Eq- 19) πΉ π―π· =πβ (πβ πΉ ππ β πΉ π© β πΉ πͺπ ) π Eq-18 πΉ π―π» =πβ (πβ πΉ ππ β πΉ π―π β π
πΊπ£ 2 ) π Eq-19
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DHW sub-systems Utility distribution sub-system (Eq- 20)
Introduction Literature review Methodology Case study Conclusion DHW sub-systems Utility distribution sub-system (Eq- 20) Process distribution sub-system (Eq- 21) πΉ π«πΌ =πβ (πβ πΉ ππ β πΉ π β πΉ πͺπ β π
πΊπ£ 2 β π
ππ‘ ) π Eq-20 πΉ ππ =πβ (πβ πΉ ππ β π
π 2 β πΉ πͺπ β π
πΊπ£ 2 ) π Eq-21
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System reliability measurement
Introduction Literature review Methodology Case study Conclusion System reliability measurement The hazard function and reliability function are determined from analysis of the failure data. So, these functions and the pattern of deterioration are dependent on the nature of components [19]. Generally, the reliability function of mechanical components mainly follows Weibull distribution. The reliability function of mechanical components mainly follows Weibull distribution (Eq-22). πΌ and π½ are scale parameter and shape parameter. π
π‘ =exp β π‘ πΌ π½ (Eq-22)[6]
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System reliability measurement (heat exchanger)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (heat exchanger) The major recorded failures in βHeat Exchangeβ are in the tube bundle, baffle plates, and gaskets. The failure data are extracted from OREDA failure handbook OREDA is an organization in Norway ,which is responsible of collecting equipment failure date from major oil companies. The sample population includes 191 heat exchangers during hours
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System reliability measurement (heat exchanger)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (heat exchanger) There are three major failure modes such as structure deficiency in the baffle plates, internal leakage in the tube bundle, and external leakage in the gasket [11]. The structure deficiency is as a result of corrosion and buckling of those plates . The internal leakage is as a result of corrosion and buckling in those tubes The external leakage in connection between shell and cap is as a result of improper gasket function. β‘
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System reliability measurement (heat exchanger)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (heat exchanger) The process of reliability function determination in components is illustrated in the following steps: Finding failure modes in components Choosing a sample, and determining the number of components in the sample Finding the number of failures in each failure mode in different time intervals Quantifying failure density function in different time intervals (π π‘ = π π π 0 β 1 βπ‘ ) determining of hazard rate in different time intervals (β π‘ = π π π π β 1 βπ‘ ) calculation of reliability function in different time interval (π
π‘ = π π π 0 ) Drawing a hazard rate diagram for the whole operation period based on available data (bathtub curve) Separation of burn-in, useful life, and wear out regions Performing regression analysis to derive suitable hazard functions, which are compatible with data trends Calculation of a reliability function in the component based on the accumulation of derived hazard functions in burn-in, useful life, and wear out regions Drawing graphs for hazard function, and reliability function.
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System reliability measurement (heat exchanger)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (heat exchanger) The reliability parameters in the heat exchanger are estimated by the regression analysis on the reliability trend ( π
2 =0.9685). The reliability function in the heat exchanger is illustrated in Eq-23 as follows: π
π‘ =exp β π‘ β‘ (Eq-23)
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System reliability measurement (boiler)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (boiler) The reliability functions in the sub-components of boiler (burner, fan, safety valve, and tube ), which follow Weibull distribution, are presented as follow: The operation of the boiler relies on the functioning of all sub-components. Therefore, the arrangement of these sub-components are defined in series. sub-component scale parameter (Ξ±) shape parameter (Ξ²) burner 1.05 fan 2.50 safety valve 1.80 tube 2.01
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System reliability measurement (boiler)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (boiler) The reliability function in the boiler is calculated by Eq-24. Reliability parameters in the boiler are estimated by the regression analysis on the reliability trend ( π
2 =0.9994), which is presented in Eq-25. π
π΅ = π
π΅π’ β π
πΉπ β π
ππ£ β π
ππ’ (Eq-24) π
π΅ π‘ =exp β π‘ β‘ (Eq-25)
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System reliability measurement
Introduction Literature review Methodology Case study Conclusion System reliability measurement the scale parameter and shape parameter of components in DHW system are given by following table [22] [23] [28] [29]. component scale parameter (Ξ±) shape parameter (Ξ²) Pipe 2.00 Pump 1.13 Gate valve 2.50 Check valve 2.60 Boiler 1.80 Heat Exchanger 2.58
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System reliability measurement (DHW system)
Introduction Literature review Methodology Case study Conclusion System reliability measurement (DHW system) The reliability parameters in the DHW system are estimated by the regression analysis on the reliability trend ( π
2 = ). The reliability function in the DHW system is illustrated in Eq-26. π
π‘ π·π»π =exp β π‘ (Eq-26)
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Sensitivity analysis (scale parameter)
Introduction Literature review Methodology Case study Conclusion Sensitivity analysis (scale parameter) The check valve is the most sensitive component in terms of scale parameter (Ξ±). the degree of sensitivity in the pump and gate valve are less than the check valve Scale parameter controls functionality, so the higher the manufacturing quality, the better the system reliability
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Sensitivity analysis (shape parameter)
Introduction Literature review Methodology Case study Conclusion Sensitivity analysis (shape parameter) The most critical component in terms of the shape parameter is the pump the degree of sensitivity in the gate valve and check valve are less than the pump The shape parameter (Ξ²) controls the rate of primary failure modes to total failure modes In terms of the shape parameter, a component is considered to be more sensitive when the rate of primary to total failure mode is decreased Also the rate indicates how sub-components have more inter-connection together
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System Availability (MTTF, MTTR)
Introduction Literature review Methodology Case study Conclusion System Availability (MTTF, MTTR) The value of MTTF and MTTR for existing components in DHW system are given by following table. The value of MTTR are extracted from the βOREDA Reliability Handbookβ and βIEEE Handbookβ. component MTTF(hour) MTTR(hour) Pipe 14.08 Pump 378.00 Gate valve 29.00 Check valve 6.00 Boiler 813.00 Heat Exchanger 24.00 Strainer 40.00
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Introduction Literature review Methodology Case study Conclusion System Availability The sequence in the βAvailability Based Maintenanceβ approach is presented as follows: Assigning different π΄ππΌ types, which identify different π π in components. Drawing π π β π‘ versus time based on different π π in order to estimate reliability parameters in each π΄ππΌ, which require for calculation of ππππΉ. Calculation of availability in each components in different π΄ππΌ types based on ππππΉ and ππππ
as well as maintenance effect. Sorting components with different π΄ππΌ types in ascending order based on maintenance effect. Calculation of availability in the system without maintenance (current availability) as a reference Performing πΎππ΄ decision process to calculate the modified availability in different combinations of components with different π΄ππΌ. Each calculation step is called βSTEP Noβ. Selecting βSTEP Noβ ,which indicates maintenance interval for all existing components.
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System Availability (AMI)
Introduction Literature review Methodology Case study Conclusion System Availability (AMI) different scenarios in terms of average maintenance intervals (yearly) in the existing components of DHW system are defined as follows: component Z0 Z1 Z2 Z3 Z4 Z5 Z6 Pipe 1.00 1.25 2.50 5.00 10.00 - Pump 12.00 Gate valve Check valve 0.25 0.50 Boiler 15.00 Heat exchanger
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System Availability (component reliability parameter)
Introduction Literature review Methodology Case study Conclusion System Availability (component reliability parameter) Pipe Boiler TM Ξ± Ξ² Ξ» MTTF R2 1.00 1.01 - 0.9990 1.25 1.02 0.9976 2.50 1.20 0.9838 5.00 1.97 0.9986 10.00 1.16 0.9999 TM(Year) Ξ± Ξ² Ξ» MTTF R2 1.00 1.85 - 0.9928 1.25 1.82 0.9945 2.50 1.90 0.9999 5.00 1.66 0.9997 10.00 1.60 0.9992 12.00 1.59 0.9998 15.00 1.61
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System Availability (component reliability parameter)
Introduction Literature review Methodology Case study Conclusion System Availability (component reliability parameter) Pump Gate valve TM(Year) Ξ± Ξ² Ξ» MTTF R2 1.00 1.07 - 0.9986 1.25 1.10 0.9992 2.50 0.9987 5.00 0.9948 10.00 0.9999 12.00 TM Ξ± Ξ² Ξ» MTTF R2 1.00 1.15 - 0.9881 1.25 1.66 0.9902 2.50 2.85 0.9923 5.00 2.31 0.9970
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System Availability (component reliability parameter)
Introduction Literature review Methodology Case study Conclusion System Availability (component reliability parameter) Check valve Heat exchanger TM(Year) Ξ± Ξ² Ξ» MTTF R2 0.25 - 0.9741 0.50 3.90 0.9894 1.00 3.10 0.9990 1.25 2.49 0.9994 2.50 2.37 0.9902 TM(Year) Ξ± Ξ² Ξ» MTTF R2 1.00 - 0.9799 1.25 0.9801 2.50 0.9895 5.00 1.10 0.9967 10.00 2.40 0.9994 12.00 3.60 0.9996
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System Availability (availability &maintenance effect)
Introduction Literature review Methodology Case study Conclusion System Availability (availability &maintenance effect)
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System Availability (sorting list)
Introduction Literature review Methodology Case study Conclusion System Availability (sorting list) STEP NO Component AMI type AMI (Year) β π π,π,π Top loop 1 H-4 Z4 10 2.063E-05 2 PI-3 Z3 5 2.708E-05 3 C-1 Z1 0.5 5.720E-05 4 C-2 Z2 7.153E-05 H-1 1.25 7.391E-05 6 PI-2 2.5 1.230E-04 7 G-1 1.309E-04 8 B-5 Z5 12 1.329E-04 9 G-2 1.350E-04 H-3 1.937E-04 11 C-3 2.351E-04 H-2 2.972E-04 13 PI-1 3.082E-04 14 P-2 7.339E-04 15 P-1 8.517E-04 16 P-4 1.374E-03 17 B-1 2.800E-03 18 P-3 4.145E-03 19 B-4 4.287E-03 20 B-2 6.269E-03 bottom loop 21 B-3 1.386E-02
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System Availability(current availability)
Introduction Literature review Methodology Case study Conclusion System Availability(current availability) The system availability is quantified based on the series structure of four sub- systems as a heating production sub-system, distribution sub-systems and a heat transfer sub-system (A= ) (Eq-27). The details of analysis are presented in the following table. system availability Sub-system 1 Sub-system 2 Sub-system 3(p) Sub-system 4 system Boiler+ Check Valve+ Pipe Gate Valve+ Check Valve+ Pump+ Pipe Gate Valve+ Heat Exchanger+ Pipe Ai π΄ π‘ = π΄ 1 β π΄ 2 β π΄ 3 β π΄ 4 (Eq-27)
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System Availability (the result of the KSA decision process)
Introduction Literature review Methodology Case study Conclusion System Availability (the result of the KSA decision process) The modified availability is quantified by the integration of existing components with different maintenance interval time( π π ) Whenever, the STEP No in the top and bottom list are the same, the calculation process will be finished. The result after running the πΎππ΄ flowchart are shown in the following table.
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System Availability (selecting βSTEP NOβ)
Introduction Literature review Methodology Case study Conclusion System Availability (selecting βSTEP NOβ) In the βSTEP Noβ selection, it is required to have the two following criteria. In each βSTEP Noβ, the maintenance plan for all existing components should be considered. The system availability in each βSTEP Noβ (modified availability) is equal to or greater than the current system availability(π΄= ). The nearest value to the average π (π= π΄ β βπ΄) is selected as a possible choice
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System Availability (selecting βSTEP NOβ)
Introduction Literature review Methodology Case study Conclusion System Availability (selecting βSTEP NOβ) The βSTEP Noβ 9T, which includes maintenance plans for all existing components in the DHW system, is the nearest point to the average of e. Comp NO:9(Top Loop) equipment MTTF (Year) MTTR (Year) TM (Year) boiler 813.00 1.00 check valve 6.00 1.25 gate valve 29.00 5.00 pump 378.00 2.50 heat exchanger 24.00 Pipe 14.08
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) It has been decided to change the arrangement of the heat transfer sub-system from parallel to standby: to diminish maintenance cost To keep the availability of the system in the same level as existing sub-system A number of assumptions in this transformation are as follows: both heat exchangers are identical failure in changeover switch is not taken into account (perfect switching). the series system, which contains the pipe, a couple of gate valves, and the heat exchanger, is replaced with a single component ( heat transfer component)
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) By regression analysis on the reliability trend of heat transfer component, a Rayleigh distribution function, which is more representative of that data trend is chosen (Eq-28a). π
π»π π‘ =ππ₯π β 4Γ 10 β8 π‘ , π²=πΓ ππ βπ (Eq-28a)
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) The reliability of the heat transfer sub-system is the summation of two events, which are illustrated in Eq-29. The main unit does not fail in the time interval (0,π‘) which denotes zero failure (π π§πππ πππππ’ππ ) The main unit does not fail until time π<π‘, and the standby unit does not fail in the time interval(π,π‘) which implies one failure (π(πππ πππππ’ππ)) . The general form of reliability function in standby (perfect switching ) is shown in Eq-30[6]. π
π π’πβπ π¦π π‘ππ = π β πΎ π‘ π‘ πΎπ π β πΎ π β π β π (π‘βπ) ππ (Eq-29) π
π π’πβπ π¦π π‘ππ = π
π (π‘)+ 0 π‘ π π π ππβ π
π (π‘βπ) (Eq-30)[6]
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) The reliability function of standby βHeat Transferβ sub-system is quantified by Eq-31 as follows: The reliability trend in standby heat transfer sub-system follows Weibull distribution (Eq-32). π
π π’πβπ π¦π π‘ππ = π β πΎ π‘ πΎ πΎπ π‘ 4 π πΎπ‘ β erf β π π‘ erf π π‘ 2 (Eq-31) π
π π’πβπ π¦π π‘ππ =exp β π‘ (Eq-32)[6]
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) The standby structure improves the reliability of the heat transfer sub-system significantly in comparison to the parallel structure.
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System Availability (Standby heat transfer sub-system)
Introduction Literature review Methodology Case study Conclusion System Availability (Standby heat transfer sub-system) The maintenance plans in the DHW system are shown in the following table. The number of maintenance in the pump and check valve are decreased as a result of improvement in the reliability of the system. The analysis outcome on the proposed system indicates a 0.76% deduction in the availability of the whole system in comparison with the existing system, which is negligible Comp NO:14(Bottom Loop)-standby equipment MTTF (Year) MTTR (Year) TM (Year) boiler 813.00 1.00 check valve 6.00 2.5 gate valve 29.00 5.00 pump 378.00 5 Heat transfer sys 24.00 2.50 Pipe 14.08
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Replacement analysis (heat exchanger sub-components)
Introduction Literature review Methodology Case study Conclusion Replacement analysis (heat exchanger sub-components) The replacement analysis is performed on both tube bundle and baffle plates based on following assumption. The maintenance period is 2.5 year ( π π =2.5) Replacement time is estimated based on modified reliability function in the heat exchanger Replacement time in parallel structure is 5 years ( π β =5) Replacement time in standby structure is 7.5 years ( π β =7.5) The rate of replacement cost to maintenance cost in the tube bundle and baffle plates are calculated as follow: sub-component C2/C1 5 years 7.5 years Tube bundle& Baffle plate 5.66E-03 8.52E-03
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Replacement analysis (LCC analysis)
Introduction Literature review Methodology Case study Conclusion Replacement analysis (LCC analysis) The maintenance and replacement cost in both the parallel and standby heat transfer sub-system is quantified by application of LCC analysis for 15 years (future value) In the parallel sub-system, future value in the heat exchanger follows Eq-34. In the standby sub-system, future value in the heat exchanger follows Eq-35. The cost items are classified in five groups: the cost of purchasing the heat exchanger(π»πΈπΆ), the unit man-hour cost (π₯) ,the cost of purchasing spare parts: the tube bundle (ππ΅), the baffle plates (π΅π), and the gasket (πΊ) πΉ=π (1+π) π (Eq-33) π ππππππππ =3.12π»πΈπΆ π₯+14.56πΊ+5.83(ππ΅+π΅π) (Eq-34) π πππππ
ππ =3.12π»πΈπΆ π₯+8.53πΊ+2.25(ππ΅+π΅π) (Eq-35)
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Introduction Literature review Methodology Case study Conclusion The aim of preventive maintenance is to increase the lifetime of the component(ππππΉ), postpone its failure, and decrease the number of failure in the system. In performing preventive maintenance, deterioration in component is expected to occur at a slower rate than the case without maintenance. The principle in proposing reliability-based optimal maintenance scheduling is to provide reliable maintenance plan along with high availability of the system, high level of safety and finally reducing maintenance cost Scale parameter (πΌ) controls the component functionality. Therefore, It can be concluded that the higher the manufacturing quality, the better the system reliability. Shape parameter(π½) controls the rate of primary failure modes to total failure modes. In terms of the shape parameter, a component is considered to be more sensitive when the rate of primary to total failure mode is decreased.
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Introduction Literature review Methodology Case study Conclusion The main outcome in availability based maintenance is to increase maintenance interval in components with low maintenance effect to prevent over- maintenance, and decrease maintenance interval in components with high maintenance effect to be more available in operation period. The result indicates that compared to the parallel structure, standby structure improves the reliability of the heat transfer sub-system. Switching from parallel to standby structure provides extra room to increase the average maintenance interval type, so the number of maintenance decreased The result of LCC analysis in both alternatives indicates that the preventive and replacement maintenance cost in standby sub-system is less than that of the parallel sub-system. Moreover, the cost of spare parts in standby sub-system is less than that of the parallel sub-system
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Questions
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System Reliability π
π‘ =exp β π‘ 7600 1.80
Reliability function in boiler is estimated based on the regression process on the reliability trend. π
π‘ =exp β π‘ π
2 =0.9994
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time interval (hour) (hour) βt failures (Baffle plate)
System Reliability time interval (hour) (hour) βt failures (Tube) failures (Baffle plate) failures (Gasket) 0-1000 2 1 3 4 17000-more 5 Total 30 32 51
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System Availability π
π β π‘ in each average maintenance interval is reduced in size in comparison with previous time period by the scaling factor(π
( π π ))
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Optimizing Maintenance plan by Availability
The ordered list is indicated as follow. Comp NO Component AMI type AMI (Year) β π π,π,π Top loop 1 H-4 Z4 10 2.063E-05 2 PI-3 Z3 5 2.708E-05 3 C-1 Z1 0.5 5.720E-05 4 C-2 Z2 7.153E-05 H-1 1.25 7.391E-05 6 PI-2 2.5 1.230E-04 7 G-1 1.309E-04 8 B-5 Z5 12 1.329E-04 9 G-2 1.350E-04 H-3 1.937E-04 11 C-3 2.351E-04 H-2 2.972E-04 13 PI-1 3.082E-04 14 P-2 7.339E-04 15 P-1 8.517E-04 16 P-4 1.374E-03 17 B-1 2.800E-03 18 P-3 4.145E-03 19 B-4 4.287E-03 20 B-2 6.269E-03 bottom loop 21 B-3 1.386E-02
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Replacement analysis The quantitative reliability values at periodic maintenance time ( π π = 2.5 π¦ππππ ) in the tube bundle and baffle plates are presented as follow: K TM (Years) Tube bundle Baffle plates R*T(t) R(t) 2.5 0.725 0.695 1 5 0.526 0.076 0.483 0.054 2 7.5 0.382 0.0001 0.336 5.54E-05 3 10 0.277 1.23E-09 0.234 8.13E-11 4 12.5 0.201 3.97E-18 0.162 1.97E-20
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Maintenance Availability
Introduction Definition System Reliability Sensitivity Analysis System Availability Maintenance Availability Standby subsystem Replacement analysis Conclusions The system reliability is compared with the reliability of existing sub- systems to identify the critical one in terms of reliability reduction. critical systems are both distribution sub-systems
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Introduction Literature review Methodology Case study Conclusion Sensitivity analysis A sensitivity analysis evaluates the impact of an independent variable as an input parameter on particular dependent variable as outcome. It is an effective tool that helps reliability engineer to predict the result of system calculation under imposing particular input variable. The value of the Weibull parameters in each component are altered in the range of -40% to 40% of its original value. In this study, the sensitivity analysis was performed on the reliability of the system at mean time to failure of current system.
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Sensitivity analysis Steps in sensitivity analysis are as follow:
Changing parameters one by one which are fluctuated in uniform increments, between the Minimum and Maximum. The final result for each change in a single parameter is collected in a plot of the outcome versus incremental changes for different input parameters. A steeply curve on a Sensitivity Plot, illustrates that the outcome of mathematical model or system is sensitive to the mentioned parameter. A relatively βflatβ curve indicates that the outcome of mathematical model or system is not sensitive to the allocated parameter.
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System Availability (selecting βSTEP NOβ)
Introduction Literature review Methodology Case study Conclusion System Availability (selecting βSTEP NOβ) The final result indicates that the revised system reliability compromises with current system reliability trend.
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