Applying Learning Outcomes to PE3001 Applied Thermodynamics & Fluid Mechanics Edmond P. Byrne
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Applying Learning Outcomes to PE3001 Applied Thermodynamics & Fluid Mechanics Edmond P. Byrne Department of Process and Chemical Engineering, University College, Cork, Ireland. Phone: +353 21 490 3094, e-mail: [email protected] Background Teaching Strategies Employed PE3001 Applied Thermodynamics & Fluid Mechanics: In attempting to achieve these learning outcomes I plan to employ a range of teaching techniques including lectures, videos as well as practicals, lab sessions and relevant props (Table 1). This is a third year module on the BE degree in Process & Chemical Engineering course which I have taught and developed over the past 7 years. It deals primarily with fluid mechanics and applied thermodynamics for process engineers. Since I have been consistently developing the module over the past 7 years, I felt I was quite happy with the module as my most ‘mature’ module. This sense was reinforced by generally very positive formal feedback from the module participants. Indeed the approach I had increasingly taken was in fact towards what I viewed as a very practical approach to fluid mechanics whereby students could fully understand the models that are used to describe fluid systems and hence employ these to design system through estimating pipeline pressure drops, flowrates and by selecting appropriate pumps for a range of circumstances, fluids and flow regimes – in other words an outcomes driven model. Nevertheless, I felt that by applying a systematic learning outcomes approach to this module, I could take my teaching and the students learning to another (higher) level and thus further improve the teaching & learning experience for all. Table 1 Teaching strategies employed Nature of flow in pipes [1] Estimating Pressure drop in: Newtonian Pipe Flow (Lam./Turb.) [2,3] Networked or branched flow [4] Non-Newtonian flow [5,6] Multiphase flow [7] Pump types, selection & design [8,9,10,11,13] Design of pump-pipeline systems [12,14] Navier-Stokes equations [15,16] Lect e.g. ☺ ☺ Vid ☺ Prop ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ ☺ Lab ☺ Key: Lect; Lecture, flow e.g.; Sample Compressible [17] and past paper problems ☺ & solutions, ☺ ☺Vid; Video clips,☺Prop; Physical props, Lab: Laboratory practicals & demonstrations. 3m 2.5m Figure 1. Does cavitation occur, and if so, at what stage? Why is this important? (LO11) Detailed Learning Outcomes for PE3001 In formulating learning outcomes (LO), I found it useful to first examine the module content and hence draw up a detailed list. This list is provided below. Students who have successfully completed PE3001 will be able to: 1. Describe the nature of flow in pipe systems and the models used to describe pipeline flow. 2. Define and solve for both primary and secondary pipe losses. 3. Apply Bernoulli’s engineering equation to any pipeline situation and hence estimate the pressure drop and/or fluid flowrate in a pipeline for a variety of fluid types and flow regimes. 4. Examine a multiple network flow system and compute both flow directions and flowrates and/or pressure drops 5. Describe the relationship between applied shear rate and shear stress in both theoretical and practical terms 6. Estimate pressure drop and/or flowrate associated with non-Newtonian flow 7. Appreciate the nature of two-phase flow and select and apply suitable models to estimate pressure drop associated with it 8. Identify all major process pump types and select suitable applications for each 9. Illustrate centrifugal pump design features and performance criteria 10. Estimate the power requirement for a pump as a function of its throughput, pressure increase and efficiency 11. Explain the reason for cavitation, its importance, how it can be avoided and estimate whether cavitation is likely to occur in a given pumping system and design such a system to ensure that it does not occur 12. Sketch the pump characteristic curve, pipeline curve, the pump-pipeline operating point and show how each of these can be altered in a practical manner 13. Derive centrifugal pump dimensionless numbers such as the Head Coefficient and Capacity Coefficient and be able to apply these (as well as the Specific Speed) to evaluate the effect of changing parameters such as pump impeller speed or size 14. Design a pump-pipeline system which deals with laminar or turbulent, single or multi-phase flow with Newtonian or non-Newtonian fluid through straight, branched or networked pipe systems 15. Apply the Navier-Stokes equations to simple systems in order to estimate pressure drop and/or flowrates using hand calculations 16. Relate how Navier-Stokes equations are used in Computational Fluid Dynamics software to solve for more complex real life applications 17. Describe the nature of high velocity compressible flow and design a choked flow nozzle Acknowledgements (a) (b) (c) Figure 2 Some props used in PE3001; (a) cross sectional cut-away of a gear pump, (b) centrifugal pump with casing and volute, (c) centrifugal pump cross-section showing impeller and rubber gasket (LO8) Succinct Learning Outcomes Having drawn up the list, I found that it was really too long and exhaustive to enter into a ‘Book of Modules’ type format. I therefore formulated a more succinct list is provided below. Participants who have completed PE3001 will be able to: 1. Assess any pipeline system with respect to pressure differentials and fluid flowrates and design a pump-pipeline system for laminar or turbulent, single or multi-phase flow of Newtonian or non-Newtonian fluid through straight, branched or networked pipe systems (1-7, 9-14) 2. Select pumps appropriate for the range of process types encountered in the process industries (8, 13) 3. Employ Navier-Stokes equations to describe simple flow systems and demonstrate how these can be applied to more complex systems using Computational Fluid Dynamics software (15-16) 4. Describe the nature of high velocity compressible flow and design a choked flow nozzle (17) Evaluating the Learning Outcomes The following evaluation techniques (Table 2) will be used in order to evaluate the learning outcomes, including the introduction of a design assignment which will evaluate learning outcome 1 above. Table 2 Evaluating learning outcomes Prac Ass CTE CAT Exam Marks: CA CA n/a CA Exam Nature of flow in pipes [1] ☺ ☺ Estimating Pressure drop in: Newtonian Pipe Flow (Lam./Turb.) ☺ ☺ ☺ [2,3] ☺ Networked or branched flow [4] ☺ ☺ Non-Newtonian flow [5,6] ☺ ☺ ☺ Multiphase flow [7] ☺ ☺ Pump types, selection & design ☺ ☺ ☺ [8,9,10,11,13] Design of pump-pipeline systems [12,14] ☺ ☺ ☺ Navier-Stokes equations [15,16] ☺ ☺ ☺ Key: Prac; Practical, Ass; Assignment (Design Problem), CTE; Class Team Exercise, CAT; Continuous Compressible flow [17] ☺ ☺ ☺ (25%), Exam (75%). Assessment Test; Exam; End of year examination. Marks: CA; Continuous Assessment Conclusions I am confident that this learning outcomes method will have the desired outcome of improving the module (teaching & learning) quality. This hypothesis will be tested through questionnaires as well as module performances from 2006-7. The author would like to thank the teaching team on the Postgraduate Diploma in Teaching & Learning in Higher Education at University College Cork.