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100110119055 FIRST LAW OF THERMODYNAMICS. CONTENTS Statement of First Law Of Thermodynamics Joule’s Experiment First law for closed system Sign convention.

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Presentation on theme: "100110119055 FIRST LAW OF THERMODYNAMICS. CONTENTS Statement of First Law Of Thermodynamics Joule’s Experiment First law for closed system Sign convention."— Presentation transcript:

1 100110119055 FIRST LAW OF THERMODYNAMICS

2 CONTENTS Statement of First Law Of Thermodynamics Joule’s Experiment First law for closed system Sign convention for heat and work transfer Mathematical expression of First law of Thermo dynamics for close system and for undergoing a cycle Conservation of mass Flow work and the energy of a flowing fluid Energy analysis of steady-flow systems Derivation of SFEE(Steady Flow Energy Equation) Some steady-flow engineering devices (Application) Energy analysis of unsteady-flow processes

3 First Law of Thermodynamics → Conservation of Energy:  Energy can be changed from one form to another, but it cannot be created or destroyed. The total amount of energy and matter in the Universe remains constant, merely changing from one form to another.  The First Law of Thermodynamics (Conservation) states that energy is always conserved, it cannot be created or destroyed. In essence, energy can be converted from one form into another.  The energy balance of a system –as a consequence of FLT- is a powerful tool to analyze the exchanges of energy between the system and surrounding. Warning: It is not correct to say that a system has a large amount of heat or a great amount of work.

4 Joule’s Experiment and the First Law of Thermodynamics. Equivalence between work and heat Schematic diagram for Joule´s experiment. Insulating walls are necessary to prevent heat transfer from the enclosed water to the surroundings. As the weights fall at constant speed, they turn a paddle wheel, which does work on water. If friction in mechanism is negligible, the work done by the paddle wheel on the water equals the change of potential energy of the weights. 1 calorie = 4.184 Joules  Work is done on water. The energy is transferred to the water – i. e. the system-. The energy transferred appears as an increase in temperature.  We can replace the insulating walls by conducting walls. We can transfer heat through the walls to the system to produce the same increase in temperature.  The increase in temperature of the system is a consequence of an increase in Internal Energy. Internal energy is a state function of the system  The sum of the heat transferred into the system and the work done on the system equals the change in the internal energy of the system

5 First law of thermodynamics for Closed Systems Reminder of a Closed System.  Closed system = Control mass  System is defined as a quantity of matter chosen for study.  No mass can cross its boundary but energy can.

6 Experience 1: W= 0  If we transfer 5 kJ of heat to a potato,  Its total energy will increase by 5 kJ.

7 Experience 2: W=0  Heat a water in a pan by transferring 15 KJ from the range.  There is 3 KJ losses.  This means E 2 -E 1 = 12 KJ.

8 Experience 3: Q=0 Heat an insulated room with electric heater., W= 5KJ (electric) means E 2 -E 1 = 5KJ. Replace the electric heater with a paddle wheel.

9 Experience 4: Q=0  If we do a 10 kJ of boundary work on a system, the system’s internal energy will increase by 10 kJ.  This is because (in the absence of any heat transfer (Q = 0), the entire boundary work will be stored in the air as part of its total energy.

10 Experience 5: Q in, Q out, W in  If we do 6 kJ of shaft work on system.  Transfer 15 kJ of heat in.  Loose 3 kJ of heat out.  Doing 4 kJ of Work out.  Then the system internal energy will increase by 14 kJ.

11 Sign Convention for heat and work transfer

12 Based on the previous experimental observations, the conservation of energy principle may be expressed as: Rate of net energy transfer by heat, work and massRate of change in total energy of the system On a rate basis

13 Usually the KE and PE are small Let us discuss the right hand side of the first law equation, i. e.  E

14 Let us turn to the Left hand side of the 1 st law equation 0 0 E mass =0 for closed system If we rearrange, we get

15 Assuming Q in >Q out and W out > W in per unit time (or on a Rate basis) KJ/s= Watt per unit mass basis (KJ/kg) differential form General Form (KJ) usually we drop the subscripts, hence The First law of thermodynamics(Mathematical)

16 KEY CONCEPT

17 First Law for a system undergoing a cycle  If the initial and the final states are exactly identical(same), then it is called cycle. – This process would not be isolated. – On a PV diagram, a cyclic process appears as a closed curve.  The internal energy must be zero since it is a state variable.

18 Perpetual motion machines Perpetual motion describes hypothetical machines that operate or produce useful work indefinitely and, more generally, hypothetical machines that produce more work or energy than they consume, whether they might operate indefinitely or not.

19 Classification of perpetual motion machine  A perpetual motion machine of the first kind  A perpetual motion machine of the second kind

20 Perpetual Motion Machine 1  A perpetual motion machine of the first kind produces work without the input of energy. It thus violates the first law of thermodynamics: the law of conservation of energy.  The law of conservation of energy is an empirical law of physics. It states that the total amount of energy in an isolated system remains constant over. A consequence of this law is that energy can neither be created nor destroyed: it can only be transformed from one state to another.  Hence, it is impossible for a machine to do the work infinitely without consuming energy.

21 CONSERVATION OF MASS Mass is conserved even during chemical reactions.  Conservation of mass: Mass, like energy, is a conserved property, and it cannot be created or destroyed during a process. Mass m and energy E can be converted to each other according to where c is the speed of light in a vacuum, which is c = 2.9979  10 8 m/s. The mass change due to energy change is absolutely negligible.

22 Control Volume A control volume differs from a closed system in that it involves mass transfer. Mass carries energy with it, and thus the mass and energy content of a system change when mass enters or leaves. Examples: Compressor,Pump,Boiler,Heat exchanger, Throttling valve, Nozzle, Diffuser etc.

23 Mass and Energy The mass and energy balances for any system undergoing any process can be expressed as

24 Continue… The mass and energy balances for any system undergoing any process can be expressed in the rate form as

25 Mass Flow Rate Mass flow through a cross section per unit time is called the mass flow rate and is denoted m. It is expressed as, where  = density, kg/m 3 (= 1/v) = average fluid velocity normal to A, m/s A= cross-sectional area, m 2

26 Continue…. The fluid volume flowing through a cross section per unit time is called the volume flow rate V. It is given by.

27 Continue.. The mass and volume flow rates are related by

28 Mass and Volume Flow Rates The average velocity V avg is defined as the average speed through a cross section.The volume flow rate is the volume of fluid flowing through a cross section per unit time. Definition of average velocity Mass flow rate Volume flow rate

29 Conservation of Mass Principle Conservation of mass principle for an ordinary bathtub.  The conservation of mass principle for a control volume: The net mass transfer to or from a control volume during a time interval  t is equal to the net change (increase or decrease) in the total mass within the control volume during  t. General conservation of mass General conservation of mass in rate form or

30 Mass Balance for Steady-Flow Processes Conservation of mass principle for a two-inlet–one-outlet steady-flow system.  During a steady-flow process, the total amount of mass contained within a control volume does not change with time (m CV = constant).  Then the conservation of mass principle requires that the total amount of mass entering a control volume equal the total amount of mass leaving it.  For steady-flow processes, we are interested in the amount of mass flowing per unit time, that is, the mass flow rate. Multiple inlets and exits Single stream  Many engineering devices such as nozzles, diffusers, turbines, compressors, and pumps involve a single stream (only one inlet and one outlet).

31 Special Case: Incompressible Flow During a steady-flow process, volume flow rates are not necessarily conserved although mass flow rates are.  The conservation of mass relations can be simplified even further when the fluid is incompressible, which is usually the case for liquids. Steady, incompressible Steady, incompressible flow (single stream)  There is no such thing as a “conservation of volume” principle.  However, for steady flow of liquids, the volume flow rates, as well as the mass flow rates, remain constant since liquids are essentially incompressible substances.

32 FLOW WORK AND THE ENERGY OF A FLOWING FLUID Schematic for flow work.  Flow work, or flow energy: The work (or energy) required to push the mass into or out of the control volume. This work is necessary for maintaining a continuous flow through a control volume. In the absence of acceleration, the force applied on a fluid by a piston is equal to force applied on piston by fluid.

33 Total Energy of a Flowing Fluid The total energy consists of three parts for a non-flowing fluid and four parts for a flowing fluid. h = u + Pv The flow energy is automatically taken care of by enthalpy. In fact, this is the main reason for defining the property enthalpy.

34 Energy Transport by Mass The product is the energy transported into control volume by mass per unit time. When the kinetic and potential energies of a fluid stream are negligible When the properties of the mass at each inlet or exit change with time as well as over the cross section

35 ENERGY ANALYSIS OF STEADY-FLOW SYSTEMS  Many engineering systems such as power plants operate under steady conditions.  Under steady-flow conditions, the mass and energy contents of a control volume remain constant.  Under steady-flow conditions, the fluid properties at an inlet or exit remain constant (do not change with time).

36 Mass and Energy balances for a steady-flow process 36 A water heater in steady operation. Mass balance Energy balance

37  Under steady operation, shaft work and electrical work are the only forms of work a simple compressible system may involve. Energy balance relations with sign conventions (i.e., heat input and work output are positive) when kinetic and potential energy changes are negligible Some energy unit equivalents

38 SOME STEADY-FLOW ENGINEERING DEVICES A modern land-based gas turbine used for electric power production. This is a General Electric LM5000 turbine. It has a length of 6.2 m, it weighs 12.5 tons, and produces 55.2 MW at 3600 rpm with steam injection.  Many engineering devices operate essentially under the same conditions for long periods of time. The components of a steam power plant (turbines, compressors, heat exchangers, and pumps), for example, operate nonstop for months before the system is shut down for maintenance. Therefore, these devices can be conveniently analyzed as steady-flow devices. At very high velocities, even small changes in velocities can cause significant changes in the kinetic energy of the fluid.

39 Nozzles and Diffusers Nozzles and diffusers are shaped so that they cause large changes in fluid velocities and thus kinetic energies.  Nozzles and diffusers are commonly utilized in jet engines, rockets, spacecraft, and even garden hoses.  A nozzle is a device that increases the velocity of a fluid at the expense of pressure.  A diffuser is a device that increases the pressure of a fluid by slowing it down.  The cross-sectional area of a nozzle decreases in the flow direction for subsonic flows and increases for supersonic flows. The reverse is true for diffusers. Energy balance for a nozzle or diffuser:

40 Turbines and Compressors  Turbine drives the electric generator In steam, gas, or hydroelectric power plants.  As the fluid passes through the turbine, work is done against the blades, which are attached to the shaft. As a result, the shaft rotates, and the turbine produces work.  Compressors, as well as pumps and fans, are devices used to increase the pressure of a fluid. Work is supplied to these devices from an external source through a rotating shaft.  A fan increases the pressure of a gas slightly and is mainly used to mobilize a gas.  A compressor is capable of compressing the gas to very high pressures. It consumes work.  Pumps work very much like compressors except that they handle liquids instead of gases. Like compressor, it also consumes work. Energy balance for the compressor in this figure:

41 Throttling valves  Throttling valves are any kind of flow-restricting devices that cause a significant pressure drop in the fluid. What is the difference between a turbine and a throttling valve? The pressure drop in the fluid is often accompanied by a large drop in temperature, and for that reason throttling devices are commonly used in refrigeration and air-conditioning applications. During a throttling process, the enthalpy of a fluid remains constant. But internal and flow energies may be converted to each other. Energy balance

42 Ideal Gas Temperature Does Not Change During a Throttling The temperature of an ideal gas does not change during a throttling(h =constant) process since h = h (T) SO…. T1=T2

43 Mixing chambers  In engineering applications, the section where the mixing process takes place is commonly referred to as a mixing chamber. The T-elbow of an ordinary shower serves as the mixing chamber for the hot- and the cold-water streams. Energy balance for the adiabatic mixing chamber in the figure is: 10  C 60  C 43  C 140 kPa

44 44 Heat exchangers  Heat exchangers are devices where two moving fluid streams exchange heat without mixing. Heat exchangers are widely used in various industries, and they come in various designs. A heat exchanger can be as simple as two concentric pipes.  Mass and energy balances for the adiabatic heat exchanger in the figure is: The heat transfer associated with a heat exchanger may be zero or nonzero depending on how the control volume is selected.

45 Pipe and duct flow  The transport of liquids or gases in pipes and ducts is of great importance in many engineering applications. Flow through a pipe or a duct usually satisfies. the steady-flow conditi Heat losses from a hot fluid flowing through an un-insulated pipe or duct to the cooler environment may be very significant. Pipe or duct flow may involve more than one form of work at the same time. Energy balance for the pipe flow shown in the figure is

46 Steady-Flow Devices Operate Steadily for Long Periods

47 47 ENERGY ANALYSIS OF UNSTEADY-FLOW PROCESSES  Many processes of interest, however, involve changes within the control volume with time. Such processes are called unsteady-flow, or transient-flow, processes.  Most unsteady-flow processes can be represented reasonably well by the uniform-flow process.  Uniform-flow process: The fluid flow at any inlet or exit is uniform and steady, and thus the fluid properties do not change with time or position over the cross section of an inlet or exit. If they do, they are averaged and treated as constants for the entire process. Charging of a rigid tank from a supply line is an unsteady-flow process since it involves changes within the control volume. The shape and size of a control volume may change during an unsteady-flow process.

48 Mass balance Energy balance The energy equation of a uniform-flow system reduces to that of a closed system when all the inlets and exits are closed. A uniform-flow system may involve electrical, shaft, and boundary work all at once.

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