WILKES UNIVERSITY MECHANICAL ENGINEERING- ENGINEERING MANAGEMENT DEPARTMENT THERMODYNAMICS - ME 322 A. GENERAL INFORMATION: Required Course for all ME & GSE majors. INSTRUCTOR: Dr. Perwez Kalim. Professor of Mechanical Engineering CONTACT INFO: SLC-139, Office Hrs: visit my webpage, Phone: 570-408-4827, Fax 570-408-7881 WEB PAGE: http://staffweb.wilkes.edu/perwez.kalim/, e-mail: Dr. K th TEXT BOOK: Fundamentals of Engr. Thermodynamics, M.J. Moran and H.N. Shapiro, J. Wiley & Sons, 8 Edn. th REFERENCE: Thermodynamics an Engineering Approach, 6 Edn, Y.A. Cengel, M.A. Boles, J. McGraw Hill. B. CATALOG DESCRIPTION: ME 322. Thermodynamics three credits, the fundamental concepts and laws of thermodynamics, thermodynamic properties of perfect and real gases, vapors, solids and liquids. Applications of thermodynamics to power cycles, and flow processes. Development of thermodynamic relationships and equations of state. Review of the first and second laws. Availability and irreversibility lecture-discussion, three hours a week. Prerequisite: MTH 112 C. LEARNING OBJECTIVES: Thermodynamics is a foundation course in the ME/EEGR curriculum and is required of all ME/EEGR students. It prepares the student to solve simple to complex problems in thermodynamics. The course presents many ideas and principles that are completely new to the student. The student will gain the ability to solve problems in a clear, and systematic way. See complete list of learning objectives. Thus the objectives of the course are to: a1. Sketch T– v, p– v, and T-s diagrams, and locate states on these diagrams. Interpolate property data from Tables. a2. Learn concepts of closed/open system, extensive and intensive properties, state, process and cycle, and apply the knowledge a3. Learn and apply ideal and non-ideal (compressible) gas laws a4. Learn conservation of mass, first and second laws of thermodynamics (energy & entropy equations). a5. Identify the differences between reversibility or irreversibility of a process and how it relates to entropy production and isentropic efficiencies c1. Apply necessary thermodynamic tools and skills such as continuity equation, energy, and entropy equations to solve real-world thermodynamic problems in engineering practice or to meet desired needs. Determine the performance of Power, Refrigeration, and Heat Pump cycles using efficiency and COP of these cycles. c2. Determine operating conditions for thermodynamic cycles in order to optimize power or efficiency c3. Design thermodynamics systems using concepts of entropy, Carnot, Rankine, and other cycles c4. Analyze valve, pump, compressor, turbine and heat exchanger boiler, condenser, nozzles, and water heaters etc. d1. Work as a team on semester long design project (Stirling engine design), make sure each student in the group participates as project grades are dependent on students’ active participation. e1. Compute changes in thermodynamic properties due to: mixing, compression, expansion, and heat exchange e2. Identify and formulate thermodynamic problems using continuity equation, first and second law of thermodynamics e3. Solve engineering problems using both ideal and non-ideal (considering compressibility) gas laws f1. Take ethical & professional responsibility during exam and design project work. Copying work of others is unethical. Grades for plagiarism, copying, or cheating will be zero irrespective of previous performance. i1. Occasionally discuss the engineering licensure (FE) issues. The students also take sample FE exam available on my website and take a quiz. k1. Use thermodynamics tools to analyze Power Cycles for improved efficiency k2. Apply both ideal and non-ideal gas laws as engineering tools necessary for engineering practice k3. Apply principles of Carnot, Rankine, and other cycles in solving engineering problems k4. Employ efficiency and coefficient of performance tools to assess performance of Power, Refrigeration, and Heat Pump cycles k5. Employ principles of thermodynamics as tools to analyze thermodynamic components such as valves, pumps, compressors, turbines and heat exchangers boiler, condenser, valves, nozzles, and water heaters etc. Combustion Engines Syllabus/Dr. kalim/Pg. 1 D. MAPPING OF THE COURSE LEARNING OUTCOMES TO ABET (Criterion 3) OUTCOMES: The Accreditation Board for Engineering and Technology (ABET) Criteria 2000 define a number of program outcomes that all graduates of ABET accredited programs must have. The course relations to these outcomes are listed below: Outcomes a, c, and e are central to the course. Knowledge of thermodynamics principles and application of mass, energy, and entropy balance, plays a very crucial role in the design of thermodynamic components and various power cycles. Outcomes d and k are addressed in the design-project component of the course. The outcome d is partially addressed by virtue that project teams are construed of students who belong to different majors. When students work on design of a thermodynamic system, processes, and power cycle, the knowledge of modern engineering tools and techniques are necessary. Outcomes f and i: They are occasionally considered in the class discussions. E. TOPICS COVERED: 1. 2. 3. 4. 5. 6. F. Temperature scales, Equations of State, First law of thermodynamics Energy analysis in closed/open systems Entropy & Second law of thermodynamics Thermodynamic processes and applications Power cycles and their applications Availability, Gibbs and Helmholtz functions (6 classes) (8 classes) (6classes) (3 classes) (9 classes) (3 classes) PREREQUISITES BY TOPIC: Knowledge of differential and integral calculus, and ability to use Word, PowerPoint & Excel is necessary. G. HOMEWORK & EXAM: Homework and pop quizzes: Class attendance is critically important as no make up quiz will be given. More than 3 unexcused absences will force the final grade to be lowered down by 0.5 grade from the maximum achievable. Unethical behavior like cheating in exam or homework, plagiarism will cost a grade of "zero" irrespective of the last performance. Each student must bring the book in the class. Bring your calculator in exams and in class. See HW schedule on website. The homework assignments will be collected only when they are announced. They may or may not be graded. If they are graded only a few problems may be selected for grading. It is student’s responsibility to do the homework after the relevant material has been discussed in class. The solutions of all assigned homework will be available on the course website. Design project: Groups must be made before February 1st. All groups will work on the Stirling Engine Project (project details may be found on internet or my website). Groups Final project reports are not required, but interim reports are required anytime by February 28th. The interim reports will not be graded. Each group work will present their work on April 23rd in the class. Three Exams will be held on February 12th, March 19th and April 23rd. Arrange your schedule now to make sure you are available on these dates as early or make-up test will not be given, unless a valid reason is presented to the instructor. All tests will be closed book unless otherwise mentioned. The grade for a missed test will be zero (0). Final Exam schedule will be announced by the Registrar. H. GRADING: Points distribution: Three Hour Exams@ 15 Pts. each = 45 Pts. Final Exam =25 Pts., Quizzes & HW =15 Pts., Project =15 Pts. Grading Scheme:4.0 (90 and ), 3.5 (85 and ), 3.0 (80 and ), 2.5 (75 and ), 2.0 (70 and ), 1.5 (65 and ), 1.0 (60 and ) and 0.0 (59 and ). The grade scale is based on the aggregate score calculated using the above distribution. Individual exams or project’s grade is not the representative of the final grade. I. METHODS OF ASSESSMENT: Graded Quiz and special HW Course Evaluations by students Prepared by: Graded Exams Design Projects Program skills surveys (performance criteria) Instructor Judgment Dr. S. Perwez Kalim Thermodynamics Syllabus/Dr. P. Kalim/Pg. 2 Good Luck and have a great semester Good Luck and let’s have a great semester Thermodynamics Syllabus/Dr. P. Kalim/Pg. 3 Thermodynamics Syllabus/Dr. P. Kalim/Pg. 4 Thermodynamics Syllabus/Dr. P. Kalim/Pg. 5 SOME BASIC CONCEPTS Thermodynamics? Capacity of hot substances to do work (therm = heat, dynamis = force, dynamics=motion) SYSTEM – OPEN (control Volume) or CLOSED, Boundary or Control Surface Thermodynamics Syllabus/Dr. P. Kalim/Pg. 6 Units Pressure, Psi and kPa, Pa = N/m2 1 bar = 105 = 100,000 Pa, 1 atm = 101.325 kPa abs. 20 psig = 20 + 14.7 Psi = 34.7 Psia 50 kPa gage = 50 + 101.325 = 151.325 kPa abs. 10 psig vacum=10+14.7 Psi=4.7 Psia 100 kPa vac = -100 + 101.325 = 1.325 kPa abs. Temperature Mass -m = kg or lb 100 oF = 100 + 460 = 560 oR Force = m*a = 100 oC = 100 + 373 = 373 oK Kg-m sec2 = Newton Thermodynamics Syllabus/Dr. P. Kalim/Pg. 7 Mass Flow rate = m = kg/sec or lb/sec = AV = density * area of inlet* inlet velocity Ideal gas Law P v = n R T, PV= mRT, n =Molar mass= Property Extensive Intensive State Process Mass Molecular Weight =density= Mass m 1 = = Volume V v P (Pa, bar) T (oC, K, oF, R), V (m3), S, H, U, (kg/m3) = 1/v U (kJ), H (kJ), S (kJ/K), KE (kJ), PE (kJ) u (kJ/kg), h (kJ/kg), s (kJ/kg-K) ke (kJ/kg), pe (kJ/kg) Two Properties define a state Path between two states make a process, P= C, T= C, V= C, Pvn= C, Pvk= C, Pv= RT, PV= mRT Cycle Two or more processes make a cycle Steady State Process P=C V=C H=C T=C Ideal gas PV = mRT Pv = RT Pv = RT P vn = C . . No storage, process not function of time, min mout Process Constant Pressure Process Constant Volume Process Constant Enthalpy or Throttling Process Constant Temperature Process Equation of state Irrev. Adiabatic Process or, Polytropic Process P vk = C Reversible Adiabatic or Isentropic Process Adiabatic Process, heat transfer Q =0 Application Condenser, Evaporator Rigid Container Valve Compression, expansion, Joule Thompson Effect Isobaric Isometic Isenthalpic Isothermal R = R /Mol Wt. R = 8.314 KJ/Kmol-K n must be determined k is known= Cp/Cv k =1.4 for air Energy Terms - Joules (N-m), Btu ( = 778 ft-lbf), Power - Watts (=Joules/sec) Kinetic KE ½ mV2 Joules Potential PE mgz Joules Heat Work Internal Enthalpy Q W U H KJ KJ KJ KJ ke pe q w u h ½ V2 J gz J J J J J Extensive Intensive = Extensive/mass Thermodynamics Syllabus/Dr. P. Kalim/Pg. 8 System and Control Volume Control Volume Air Conditioning Systems, Turbine/Pump/Compressor Design And Many others Single Interpolation- Volume m3/kg Temperature oC Volume m3/kg 130 1.0697*10-3 140 1.0797*10-3 What is the Volume at 134 oC? 10 oC diff = 0.0100 * 10-3 m3/kg o -3 3 1 C diff = 0.00100 * 10 m /kg o for 4 C diff = 0.00400 * 10-3 @ 134 oC volume is = 0.00400 * 10-3 + 1.0697 * 10-3 = 1.0737 * 10-3 m3/kg PURE SUBSTANCE. LATENT HEAT, PHASES Double Interpolation - Volume m3/kg Temperature oC Pressure, 4 bars Pressure, 5 bars 120 0.06546 0.05193 140 0.06913 0.05492 First interpolate Volume at Then interpolate Volume 4 bars and 130 oC at 5 bars and 130 oC = 0.067295 = 0.053425 Determine volume at 130 o C and 4.5 bars Then interpolate between 4 and 5 bars = 0.06036 m3/kg Critical Point Pc, Tc P = C line Subcooled or compressed Region 560 oC 4s 4 1 T=C, P = C T 560 oC, 200 bars Superheated Vapor Region Liquid-Vapor Region, X X = 45 % S=C Sat. Liquid Line Uf, vf, hf, sf V=C S C 2s 2 Sat. Vapor Line ug, vg, hg, sg T=C, P = C 3 0.2 bars, 60 oC S Or V Thermodynamics Syllabus/Dr. P. Kalim/Pg. 9
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