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3 rd Research Week 2009 – 2010 Sustainable Green Intelligent Innovative Island Doctoral Consortium E – Poster

3 rd Research Week 2009 – 2010 Sustainable Green Intelligent Innovative Island Doctoral Consortium E – Poster. Sensitivity Analysis and Parameter Optimization of a Heat Loss Model for a Composting System. A CKMEZ M UDHOO

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3 rd Research Week 2009 – 2010 Sustainable Green Intelligent Innovative Island Doctoral Consortium E – Poster

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  1. 3rd Research Week 2009–2010Sustainable Green Intelligent Innovative IslandDoctoral Consortium E–Poster Sensitivity Analysis and Parameter Optimization of a Heat Loss Model for a Composting System ACKMEZ MUDHOO Department of Chemical & Environmental Engineering Faculty of Engineering, University of Mauritius. Master of Philosophy Research Supervisor: Professor Romeela MOHEE Faculty of Engineering

  2. MUDHOO, A. AND MOHEE, R., 2006. Sensitivity analysis and parameter optimization of a heat loss model for a composting system. Journal of Environmental Informatics, 8(2), 100–110.doi:10.3808/jei.200600080 MUDHOO, A. AND MOHEE, R., 2008. Modeling heat loss during self–heating composting based on combined fluid film theory and boundary layer concepts.Journal of Environmental Informatics, 11(2), 74–89. doi:10.3808/jei.200800113 The following presentation is distilled from the research papers given below and which have been published for the MPhil Research

  3. Abstract A combined multi-parameter sensitivity analysis/frequency array analysis technique was employed to assess the impact of design conditions and matrix-specific properties on the rate of heat loss from a self-heating composting process. This method was specifically used to identify the range of parameters over which a model predicting the overall heat-transfer coefficients (U-values) for the heat loss process are particularly sensitive. The model was found to be most sensitive for the following range of input parameters: the internal diameter of reactor varying from 0.8m to 1.2m, the combined reactor wall and insulation thickness ranging from 4cm to 6cm, the free airspace of the matrix varying from 50% to 60%, the reactor length varying from 1.0m to 1.5m, the thermal conductivity of the organic substrates ranging from 0.1W/m.K to 0.2W/m.K and the preferred thermal conductivity of the insulation material being less than 0.2W/m.K. This analysis disclosed the matrix free airspace, the internal diameter of the reactor and the combined thickness of reactor wall and insulation as the most important parameters which should be given high priority when designing in-vessel compost reactors.

  4. Introduction The composting process has been extensively studied and numerous mathematical models have been developed to describe the heat dynamics and heat loss mechanisms. However, no data on a combined sensitivity analysis and optimization of the numerous parameters involved in these models has been explicitly reported in compost literature.

  5. Research objectives Hence, the objective of this study was to assess the sensitivity of a corrected form of the Thermal Resistance Pathway (TRP) model to the input parameters over a range of values that have been observed in practice for various composts. A combined multi-parameter sensitivity analysis (MPSA) and frequency array/frequency analysis technique has been used and a preliminary parameter optimization has also been conducted. The end results are intended to assist in the redesign of a compost bioreactor that could prolong the duration of the thermophilic temperatures within the matrix, and hopefully improve the biodegradation rates during the initial stages of the composting process.

  6. Details of the self-heating bioreactor used for the composting experiment

  7. Conceptual schematic of TRP-model for section of compost in reactor

  8. TRP Model Formulation U=overall heat-transfer coefficient (W/m2.K) Cf,opt=optimum correction factor (positive numerical constant, 10.812) Aco=outside surface area of cylinder (m2) Aci=inside surface area of cylinder (m2) hwsi=film heat transfer coefficient in water condensate film on inner surface area of cylinder (W/m2 .K) ho=convective heat transfer coefficient between outside surface of reactor and room (W/m2.K) ro=inner radius of bioreactor from centre to inner surface (m) ri=inner radius of compost material which is at constant temperature (m) L=reactor length (m) X=thickness of reactor wall with insulation (m) Ks=thermal conductivity of compost bed material (W/m.K) K=thermal conductivity of wall material (typically PVC)(W/m.K)

  9. Parameter Identification & Discretization Pf , Po=high and low endpoints of the parameter range, respectively N = Number of intervals in range = 6 (N= 1, 2, 3,4, 5, 6)  = multiplier The values of the parameter were then calculated from:

  10. Upper and lower bound and discretized parameter values tested in Multi-Parameter Sensitivity Analysis

  11. Multi-Parameter Sensitivity Analysis An approach that can be employed to assess model response is to use a combined multi-parameter sensitivity analysis and frequency array or graphical approach. Technique has been used to assess emissions from sewer systems for determining the relative importance of factors influencing the natural attenuation of mining contaminants and in quantifying the importance of the parameters in models developed to describe the fate of volatile organic compounds in trickling filters. MPSA approach allows an assessment of the importance of each input parameter at a variety of settings of the other input parameters and thus provides a more realistic picture than standard analyses. Standard analyses assess each input parameter only at the default values of the other parameters while in MPSA, a pairwise evaluation of the parameters is performed to allow for the development of three-dimensional response curves. For the evaluation of a given pair of parameters (primary parameters), all of the non-selected parameters are designated secondary parameters. At each combination of the primary parameters, the model is evaluated for all of the combinations of the secondary parameters. To reduce the number of responses obtained for each combination of the primary parameters to a single value, a removal criterion (criterion of exceedance) is defined. The frequency array plot generated provides an indication of the potential for obtaining a significant response for a given combination of the primary parameters.

  12. Frequency array plots & Primaryparameter pairs For a chosen pair out of the 7 selected primary parameter pairs, a total of 49 combinations are possible among the values. Selecting a pair of primary parameters leaves out five secondary parameters. The corresponding total number of combinations of secondary parameters that can be tested for a single combination of primary parameters is 75 (16807). Total number of combinations for simulations = 823543 The comparisons within categories were identified on the basis of potential competition between the specific category parameters. For example, variations in L and Dmight compete to determine the geometrical design of the reactor, and thence control the volume of substrates that can be composted. The comparisons between categories have been selected on the basis of likely interaction between the parameters

  13. Primary parameter pairs tested in MPSA & Frequency Array Analysis A program was written in MATLAB7.0 to evaluate the U-values for each and every combination of the seven mathematical equation parameters. All the possible combinations were deduced using a Trellis Search algorithm embedded in the program. For each combination of a primary parameter pair, the U-values obtained were screened for the criterion of exceedance, and all values exceeding this criterion (E) were enumerated. The total obtained was divided by 16807, and the resultant value (f) plotted against the corresponding primary parameters on a three-dimensional plot using the SigmaPlot9.0 software (2004 SYSTAT Software, Inc.)

  14. Steps in the MPSA

  15. Criteria for exceedance In most composting experiments, the objective is to maintain thermophilic temperatures (45°C to 60°C) for 3 to 4 days, allow an optimum biodegradation to take place through optimum microbial activity and thus ensure maximum stabilization and sanitization of the organic matter High U-values during the active thermophilic stage (metabolic heat output is normally most during this stage) will cause higher rates of heat loss and reduce the duration of the thermophilic temperatures in the compost matrix. Relatively low U-values would be preferred in composting. As such, the criteria for exceedance of different responses for different compost matrices will have different values. Thus, the choice of E becomes particularly arbitrary. Hence, for the selected comparisons of primary parameters, E has been varied to assess its impact on the conclusions drawn from the frequency array plots. For a minimum U-value of 0.14 W/m2·K and a maximum of 58.01 W/m2·K obtained after evaluation of all combinations, 14 U-values have been tested for the seven primary parameter pairs. These values have been calculated by dividing the range 0.14 to 58.01 W/m2·K into 13 equal intervals. Based on the frequency array plots that were generated for these U-values, the exceedance criteria retained for further analysis were 4.5, 13.5 and 23.0 W/m2·K

  16. Criteria for Exceedance Basic concept of sensitivity analysis using a hypothetical equation with only two parameters

  17. Results – Frequency Array Plots

  18. Results – Frequency Array Plots

  19. SUMMARY Specific range of values for design and substrate parameters of compost reactor determined from a combined MPSA & Frequency array analysis Results – Frequency Array Plots

  20. Analysis of the impact of Exceedance Criteria The frequency array technique required the definition of an exceedance criterion against which equation estimates were compared. In this study, values were selected to represent the responses that would be considered substantial and significant within the context of assessing the rate of heat loss from a self-heating composting matrix. It is apparent, however, that the selection of these criteria might have had some influence on the conclusions extracted from the plots. An analysis of all the frequency array plots for the seven primary parameter pairs for E = 4.5, 13.5 and 23.0 W/m2·K was therefore performed. The only substantial difference between the plots was the relative magnitude of the frequency values, with the lower values observed for the case that had a higher exceedance criterion. This was to be expected, as fewer combinations of the parameters would be expected to exceed the higher criterion. Similar conclusions were reached with respect to the sensitivity to parameter values from every frequency array plot. The results therefore suggested that the conclusions drawn with respect to the equation’s sensitivity to the parameters appeared to be independent of the exceedance criterion over the range of parameter values considered in this study.

  21. Conclusions The combined multi-parameter sensitivity analysis and frequency array method (MPSA/FAM) has been employed to perform a screening study that identified the most sensitive ranges of parameters for a mathematical equation that could be used to evaluate the overall heat transfer coefficients for the in-vessel self-heating composting of mixed organic substrates. The conclusions reached using this technique were found to be reasonably consistent over a range of exceedance criteria that are of practical interest (4.5, 13.5 and 23.0 W/m2·K). The optimum ranges of values for the latter parameters as revealed from the MPSA/ FAM are 50% to 60% (FAS), 0.04 m to 0.06 m (thickness) and 0.8 to 1.2 m (internal diameter). The set of information obtained from the MPSA/FAM can be used to identify design and operating strategies that might be employed to minimize excessive heat losses during the initial thermophilic stages of the composting process. Furthermore, despite the fact that this technique generally requires extensive computational power, the end results provide a reliable guide for future data-collection efforts and to order research priorities. The present analysis could be substantiated with a further reasonably realistic COMPUTATIONAL FLUID DYNAMICS analysis of the Heat Transfer Mechanisms operating in the compost matrix.

  22. THANK YOU FOR YOUR ATTENTION Ackmez Mudhoo B.Eng., LCIWM Department of Chemical & Environmental Engineering Faculty of Engineering, University of Mauritius - Réduit, Mauritius ackmezchem@yahoo.co.uk Tel. (+230) 403 7772 (Office); Fax (+230) 465 7144

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