A Systems Dynamics Enabled Real-Time Efficiency for Fuel Cell Data-Driven Remanufacturing
Abstract
:1. Introduction and Related Research
Technical Status of Fuel Cells
2. Remanufacturing and Industry 4.0
3. Overview of Terms and Terminology Important in This Research
3.1. System Dynamics Modelling and Its Application for Automotive Systems
3.2. Parameters for Remanufacturing
3.3. Fuel Cells and Remanufacturing
3.4. Real-Time Efficiency in Remanufacturing
4. Materials and Methods
4.1. Semi-Structured Interviews
4.2. Case Companies’ Profiles
4.3. Data Collection
5. Analysis and Discussion
5.1. Pareto Analysis of (Data-Driven) Remanufacturing Variables
- Vibration data: The data collected from the sensor placed on the BMS, which collects information on the physical state of the fuel cell.
- Time of cycle run: This is the time which the fuel cell is in operation in seconds, s.
- Traditional remanufacturing: As described in Table 1, this is the parameters of variables currently employed in remanufacturing for non-sensor enabled parts, for example vehicle gearboxes.
- Tank current, Tank/c: The current values of the hydrogen tank in Amps, A.
- Cell voltage, Cell/v: The voltage of the individual fuel cells, V.
- Tank temperature, Tank/t: The temperature captured for the hydrogen tank, in degree centigrade, °C.
- Distance from OEM to 3rd party remanufacturer, DFOtoReman: The distance in kilometres, km, from the OEM to the 3rd party remanufacturer’s site.
- Distance from 3rd party remanufacturer to suppliers, DfRtoSup: The distance in kilometres, km, from the 3rd party remanufacturer to suppliers. It is assumed that there is more than one supplier.
- Hydrogen usage quantity: The quantity of hydrogen used in the fuel cell during operation. This is calculated in grams, g.
- Cell temperature: The temperature of the fuel cell, in degree centigrade, °C.
- Tank pressure, Tank/p: The pressure in Pa, of the hydrogen tank.
- Inlet pressure: The pressure in Pa, at the inlet of the hydrogen tank.
- Air flow: The air flow of the entire system measured in cubic feet per minute (CFM).
- Stack voltage: The voltage of the stack of fuel cells. It is measured in volts, V.
5.2. Dynamic Implications of Data for Remanufacturing
- That the remanufacturing variables shall be analysed based on their process data, and not their processes.
- That, for simplicity’s sake, these data shall be analysed as “data from sensors” (for example, vibration data and stack voltage, etc.) and “data from other sources” (for example, data from traditional remanufacturing parameters).
5.3. Coding the Simulation Model
- Rate of entry of components to be remanufactured = Random, between 1 and 3 h.
- Percentage of components with information = 5% (we take a pessimistic baseline situation, as if the majority of components have no information)
- Percentage of components without information (it is assumed that some components without information are also entered into the system; those that are physically inspected) = 95%.
- Inspection time per component (for those components with information) = We use triangular distribution (3, 5, 7) min. While a component may have data about it, it is important to still carry out some physical examination to confirm that it is fit for remanufacturing. This is akin to a verification inspection. We estimate a triangular distribution with min = 3 min, max = 7 min and mode = 5 min.
- Inspection time per component (for those components without information) = Triangular distribution (30, 60, 45) min is used. We estimate a triangular distribution with min = 30 min; max = 60 min and mode = 45 min.
- Remanufacturing time per component = Triangular (2, 3, 5) h. We estimate a triangular distribution with min = 2 h, maximum = 5 h and mode = 3 h.
- Remanufacturing capacity = we assume 1 set of machines.
- Percentage of components (i.e., those without information) that are not remanufactured after inspection (since it is possible that some components will be found not to be “remanufacturable” after inspecting them physically) = 70%. Hence, components that are remanufactured after they are physically inspected constitute 30% of the total.
6. Simulation Results
- Continue with the current capacity, but allow the components with information to vary such that capacity is not stretched. In such a situation, when capacity utilisation is approaching a high level (say, 80%), the components with information are reduced, so as not to overburden the system. When there is slack, more components with information can be entered into the system.
- Ensure all components have information and determine (through simulation) the capacity that is needed to ensure that capacity is not overstretched or underutilised.
7. Conclusions
Limitations and Further Research
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
Nomenclature
BMS | Battery Management System |
CLD | Causal Loop Diagram |
CBM | Condition-Based Monitoring |
CE | Circular Economy |
DFOtoReman | Distance from OEM to 3rd Party Remanufacturer |
DfRtoSup | Distance from 3rd Party Remanufacturer to Supplier |
EOL | End-Of-Life |
FC | Fuel Cell |
FCEVs | Fuel Cell for Electric Vehicles |
FCR | Fuel Cell Recovery |
OEM | Original Equipment Manufacturer |
I4.0 | Industry 4.0 |
SFD | Stock and Flow Diagram |
V | Voltage |
Min | Minimum |
Max | Maximum |
Reman | Remanufacturing |
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Parameters for Reman | Definition | Reference |
---|---|---|
Interchangeability of parts | Product must be made up of standard interchangeable parts | Lund (1998) [28] |
Can be dissembled | The product has parts that can be disassembled and then reassembled after remanufacture. | Ijomah (2007) [11] |
Availability of core | Core part of product which should be disassembled for re- manufacturing must be available. | Hatcher (2011) [6] |
Low cost of core | The cost of obtaining and reprocessing the core parts is low in comparison to the remaining value added | Lund (1998) [28], Hauser and Lund (2008) [10] |
Technology for remanufacture | Availability of technology for remanufacture | Nasr and Thurston (2006) [67] |
Marketability | Available market for remanufactured product. | Ayres R. et al. (1997) [68] |
Upgradability | Having the potential to be upgraded | Shu and Flowers (1998) [69] |
Reverse flow | There are channels available for reverse flow of used product | Ayres et al. [68] |
Length of life cycle | Product technology is stable over more than one life cycle | Lund (1984) [7] |
Respond. 1 | Respond. 2 | Respond. 3 | Respond. 4 | Respond. 5 | Respond. 6 |
---|---|---|---|---|---|
Stack temperature voltage, variables required for traditional remanufacturing | Distance from OEM to 3rd party reman., distance from 3rd party reman to spares suppliers | Distance from OEM to 3rd party reman, distance from 3rd party reman to spares suppliers | Parameters required in traditional remanufacturing for automobile | Stack and individual cells voltage, temperature, current, air flow, vibration data captured in battery cage, time of cycle run | Hydrogen tank temperature, tank pressure, inlet pressure, hydrogen usage quantity, blower current |
Variables | Respond. 1 | Respond. 2 | Respond. 3 | Respond. 4 | Respond. 5 | Respond. 6 | Total |
---|---|---|---|---|---|---|---|
Trad reman. | 3 | 5 | 5 | 5 | 5 | 3 | 26 |
Stack/v | 4 | 3 | 3 | 2 | 5 | 3 | 20 |
Stack/c | 5 | 2 | 1 | 2 | 4 | 5 | 19 |
Stack/t | 4 | 3 | 1 | 2 | 4 | 3 | 17 |
Cell/v | 4 | 4 | 3 | 3 | 4 | 5 | 23 |
Cell/c | 3 | 2 | 2 | 1 | 5 | 5 | 18 |
Cell/t | 4 | 3 | 3 | 3 | 5 | 4 | 22 |
Tank/t | 4 | 2 | 4 | 3 | 5 | 5 | 23 |
Tank/v | 3 | 1 | 2 | 3 | 5 | 5 | 19 |
Tank/c | 5 | 4 | 4 | 3 | 5 | 5 | 26 |
Tank/p | 3 | 5 | 2 | 3 | 4 | 5 | 22 |
Inlet Pressure | 3 | 2 | 3 | 4 | 5 | 4 | 21 |
Vibration data | 4 | 5 | 5 | 5 | 5 | 5 | 29 |
DFOtoReman | 2 | 5 | 5 | 5 | 3 | 3 | 23 |
DFRtoSup | 3 | 5 | 5 | 5 | 3 | 2 | 23 |
Air flow | 4 | 3 | 2 | 3 | 4 | 5 | 21 |
Time of cycle run | 5 | 5 | 5 | 5 | 4 | 4 | 28 |
Hydrogen usage qty. | 4 | 3 | 4 | 3 | 4 | 5 | 23 |
Blower current | 3 | 2 | 2 | 4 | 4 | 4 | 19 |
Current Status | Components with Information Are Allowed to Vary | All Components Have Information and Capacity Is Doubled | |
---|---|---|---|
Average remanufacturing cycle time (min) | 306 | 350 | 225 |
Number of remanufactured components | 1474 | 2096 | 4385 |
Average capacity utilisation | 56% | 80% | 81% |
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Okorie, O.; Salonitis, K.; Charnley, F.; Turner, C. A Systems Dynamics Enabled Real-Time Efficiency for Fuel Cell Data-Driven Remanufacturing. J. Manuf. Mater. Process. 2018, 2, 77. https://doi.org/10.3390/jmmp2040077
Okorie O, Salonitis K, Charnley F, Turner C. A Systems Dynamics Enabled Real-Time Efficiency for Fuel Cell Data-Driven Remanufacturing. Journal of Manufacturing and Materials Processing. 2018; 2(4):77. https://doi.org/10.3390/jmmp2040077
Chicago/Turabian StyleOkorie, Okechukwu, Konstantinos Salonitis, Fiona Charnley, and Christopher Turner. 2018. "A Systems Dynamics Enabled Real-Time Efficiency for Fuel Cell Data-Driven Remanufacturing" Journal of Manufacturing and Materials Processing 2, no. 4: 77. https://doi.org/10.3390/jmmp2040077
APA StyleOkorie, O., Salonitis, K., Charnley, F., & Turner, C. (2018). A Systems Dynamics Enabled Real-Time Efficiency for Fuel Cell Data-Driven Remanufacturing. Journal of Manufacturing and Materials Processing, 2(4), 77. https://doi.org/10.3390/jmmp2040077