2021-12-23 17:28:35 +00:00
|
|
|
---
|
|
|
|
author: Alvie Rahman
|
|
|
|
date: \today
|
|
|
|
title: MMME1048 // Thermodynamics
|
|
|
|
tags: [ uni, nottingham, mechanical, engineering, mmme1048, thermodynamics ]
|
|
|
|
---
|
|
|
|
|
|
|
|
# What is Thermodynamics?
|
|
|
|
|
|
|
|
Thermodynamics deals with the transfer of heat energy and temperature.
|
|
|
|
|
|
|
|
# Concepts and Definitions
|
|
|
|
|
|
|
|
## System
|
|
|
|
|
|
|
|
A region of space, marked off by its boundary.
|
|
|
|
It contains some matter and the matter inside is what we are investigating.
|
|
|
|
|
|
|
|
There are two types of sysems:
|
|
|
|
|
|
|
|
- Closed systems
|
|
|
|
|
|
|
|
- Contain a fixed quantity of matter
|
|
|
|
- Work and heat cross bounaries
|
|
|
|
- Impermeable boundaries, some may be moved
|
|
|
|
- Non-flow processes (no transfer of mass)
|
|
|
|
|
|
|
|
- Open systems
|
|
|
|
|
|
|
|
- Boundary is imaginary
|
|
|
|
- Mass can flow in an out (flow processes)
|
|
|
|
- Work and heat transfer can occur
|
|
|
|
|
|
|
|
## Equilibrium
|
|
|
|
|
|
|
|
The system is in equilibrium if all parts of the system are at the same conditions, such as pressure
|
|
|
|
and temperature.
|
|
|
|
|
|
|
|
The system is not in equilibrium if parts of the system are at different conditions.
|
|
|
|
|
|
|
|
#### Adiabatic
|
|
|
|
|
|
|
|
A process in which does not cross the system boundary
|
|
|
|
|
2021-12-23 21:00:18 +00:00
|
|
|
## Perfect (Ideal) Gasses
|
|
|
|
|
|
|
|
A perfect gas is defined as one in which:
|
|
|
|
|
|
|
|
- all collisions between molecules are perfectly elastic
|
|
|
|
- there are no intermolecular forces
|
|
|
|
|
|
|
|
Perfect gases do not exist in the real world and they have two requirements in thermodynamics:
|
|
|
|
|
|
|
|
### The Requirements of Perfect Gasses
|
|
|
|
|
|
|
|
#### Obey the Perfect Gas Equation
|
|
|
|
|
|
|
|
$$pV = n \tilde R T$$
|
|
|
|
|
|
|
|
where $n$ is the number of moles of a substance and $\tilde R$ is the universal gas constant
|
|
|
|
|
|
|
|
or
|
|
|
|
|
|
|
|
$$pV =mRT$$
|
|
|
|
|
|
|
|
where the gas constant $R = \frac{\tilde R}{\tilde m}$, $\tilde m$ is molecular mass
|
|
|
|
|
|
|
|
or
|
|
|
|
|
|
|
|
$$pv = RT$$
|
|
|
|
|
|
|
|
(using the specific volume)
|
|
|
|
|
|
|
|
#### $c_p$ and $c_v$ are constant
|
|
|
|
|
|
|
|
This gives us the equations:
|
|
|
|
|
|
|
|
$$u_2 - u_1 = c_v(T_2-T_1)$$
|
|
|
|
|
|
|
|
$$h_2 - h_1 = c_p(T_2-T_1)$$
|
|
|
|
|
|
|
|
### Relationship Between Specific Gas Constant and Specific Heats
|
|
|
|
|
|
|
|
$$c_v = \frac{R}{\gamma - 1}$$
|
|
|
|
|
|
|
|
$$c_p = \frac{\gamma}{\gamma -1} R$$
|
|
|
|
|
|
|
|
<details>
|
|
|
|
<summary>
|
|
|
|
|
|
|
|
#### Derivation
|
|
|
|
|
|
|
|
</summary>
|
|
|
|
|
|
|
|
We know the following are true (for perfect gases):
|
|
|
|
|
|
|
|
$$\frac{c_p}{c_v} = \gamma$$
|
|
|
|
|
|
|
|
$$u_2 - u_1 = c_v(T_2-T_1)$$
|
|
|
|
|
|
|
|
$$h_2 - h_1 = c_p(T_2-T_1)$$
|
|
|
|
|
|
|
|
So:
|
|
|
|
|
|
|
|
\begin{align*}
|
|
|
|
h_2 - h_1 &= u_2 - u_1 + (p_2v_2 - p_1v_1) \\
|
|
|
|
c_p(T_2-T_1) &= c_v(T_2-T_1) + R(T_2-T_1) \\
|
|
|
|
c_p &= c_v + R \\
|
|
|
|
\\
|
|
|
|
c_p &= c_v \gamma \\
|
|
|
|
c_v + R &= c_v\gamma \\
|
|
|
|
c_v &= \frac{R}{\gamma - 1} \\
|
|
|
|
\\
|
2021-12-23 21:49:38 +00:00
|
|
|
\frac{c_p}{\gamma} &= c_v \\
|
2021-12-23 21:00:18 +00:00
|
|
|
c_p &= \frac{c_p}{\gamma} + R \\
|
|
|
|
c_p &= \frac{\gamma}{\gamma -1} R
|
|
|
|
\end{align*}
|
|
|
|
|
|
|
|
|
|
|
|
</details>
|
|
|
|
|
|
|
|
|
2021-12-23 17:28:35 +00:00
|
|
|
## Properties of State
|
|
|
|
|
|
|
|
*State* is defined as the condition of a system as described by its properties.
|
|
|
|
The state may be identified by certain observable macroscopic properties.
|
|
|
|
These properties are the *properties of state* and they always have the same values for a given
|
|
|
|
state.
|
|
|
|
|
|
|
|
A *property* can be defined as any quantity that depends on the *state* of the system and is
|
|
|
|
independant of the path by which the system arrived at the given state.
|
|
|
|
Properties determining the state of a thermodynamic system are referred to as *thermodynamic
|
|
|
|
properties* of the *state* of the system.
|
|
|
|
|
|
|
|
Common properties of state are:
|
|
|
|
|
|
|
|
- Temperature
|
|
|
|
- Pressure
|
|
|
|
- Mass
|
|
|
|
- Volume
|
|
|
|
|
|
|
|
And these can be determined by simple measurements.
|
|
|
|
Other properties can be calculated:
|
|
|
|
|
|
|
|
- Specific volume
|
|
|
|
- Density
|
|
|
|
- Internal energy
|
|
|
|
- Enthalpy
|
|
|
|
- Entropy
|
|
|
|
|
|
|
|
### Intensive vs Extensive Properties
|
|
|
|
|
|
|
|
In thermodynamics we distinguish between *intensive*, *extensive*, and *specific* properties:
|
|
|
|
|
|
|
|
- Intensive --- properties which do not depend on mass (e.g. temperature)
|
|
|
|
- Extensive --- properties which do depend on the mass of substance in a system (e.g. volume)
|
|
|
|
- Specific (extensive) --- extensive properties which are reduced to unit mass of substance
|
|
|
|
(essentially an extensive property divided by mass) (e.g. specific volume)
|
|
|
|
|
2021-12-23 21:00:18 +00:00
|
|
|
### Units
|
2021-12-23 17:28:35 +00:00
|
|
|
|
2021-12-23 21:49:38 +00:00
|
|
|
<div class="tableWrapper">
|
|
|
|
|
2021-12-23 17:28:35 +00:00
|
|
|
Property | Symbol | Units | Intensive | Extensive
|
|
|
|
--------------- | ------ | --------------- | --------- | ---------
|
|
|
|
Pressure | p | Pa | Yes |
|
|
|
|
Temperature | T | K | Yes |
|
|
|
|
Volume | V | m$^3$ | | Yes
|
|
|
|
Mass | m | kg | | Yes
|
2021-12-23 21:00:18 +00:00
|
|
|
Specific Volume | v | m$^3$ kg$^{-1}$ | Yes |
|
2021-12-23 17:28:35 +00:00
|
|
|
Density | $\rho$ | kg m$^{-3}$ | Yes |
|
|
|
|
Internal Energy | U | J | | Yes
|
|
|
|
Entropy | S | J K$^{-1}$ | | Yes
|
|
|
|
Enthalpy | H | J | | Yes
|
|
|
|
|
2021-12-23 21:49:38 +00:00
|
|
|
</div>
|
|
|
|
|
2021-12-23 21:00:18 +00:00
|
|
|
### Density
|
|
|
|
|
|
|
|
For an ideal gas:
|
|
|
|
|
|
|
|
$$\rho = \frac{p}{RT}$$
|
|
|
|
|
|
|
|
### Enthalpy and Specific Enthalpy
|
|
|
|
|
|
|
|
Enthalpy does not have a general physical interpretation.
|
|
|
|
It is used because the combination $u + pv$ appears naturally in the analysis of many
|
|
|
|
thermodynamic problems.
|
|
|
|
|
|
|
|
The heat transferred to a closed system undergoing a reversible constant pressure process is equal
|
|
|
|
to the change in enthalpy of the system.
|
|
|
|
|
|
|
|
Enthalpy is defined as:
|
|
|
|
|
|
|
|
$$H = U+pV$$
|
|
|
|
|
|
|
|
and Specific Enthalpy:
|
|
|
|
|
|
|
|
$$h = u + pv$$
|
|
|
|
|
|
|
|
### Entropy and Specific Entropy
|
|
|
|
|
|
|
|
Entropy is defined as the following, given that the process s reversible:
|
|
|
|
|
|
|
|
$$S_2 - S_1 = \int\! \frac{\mathrm{d}Q}{T}$$
|
|
|
|
|
|
|
|
### Heat Capacity and Specific Heat Capacity
|
|
|
|
|
|
|
|
Heat capacity is quantity of heat required to raise the temperature of a system by a unit
|
|
|
|
temperature:
|
|
|
|
|
|
|
|
$$C = \frac{\mathrm{d}Q}{\mathrm{d}T}$$
|
|
|
|
|
|
|
|
Specific heat capacity is the quantity of heat required to raise the temperature of a unit mass
|
|
|
|
substance by a unit temperature:
|
|
|
|
|
|
|
|
$$c = \frac{\mathrm{d}q}{\mathrm{d}T}$$
|
|
|
|
|
|
|
|
<details>
|
|
|
|
<summary>
|
|
|
|
|
|
|
|
#### Heat Capacity in Closed Systems and Internal Energy
|
|
|
|
|
|
|
|
The specific heat transfer to a closed system during a reversible constant **volume** process is
|
|
|
|
equal to the change in specific **internal energy** of the system:
|
|
|
|
|
|
|
|
$$c_v = \frac{\mathrm{d}q}{\mathrm{d}T} = \frac{\mathrm{d}u}{\mathrm{d}T}$$
|
|
|
|
|
|
|
|
</summary>
|
|
|
|
|
|
|
|
This is because if the change in volume, $\mathrm{d}v = 0$, then the work done, $\mathrm{d}w = 0$
|
|
|
|
also.
|
|
|
|
So applying the (1st Corollary of the) 1st Law to an isochoric process:
|
|
|
|
|
|
|
|
$$\mathrm{d}q + \mathrm{d}w = \mathrm{d}u \rightarrow \mathrm{d}q = \mathrm{d}u$$
|
|
|
|
|
|
|
|
since $\mathrm{d}w = 0$.
|
|
|
|
|
|
|
|
</details>
|
|
|
|
|
|
|
|
<details>
|
|
|
|
<summary>
|
|
|
|
|
|
|
|
#### Heat Capacity in Closed Systems and Enthalpy
|
|
|
|
|
|
|
|
The specific heat transfer to a closed system during a reversible constant **pressure** process is
|
|
|
|
equal to the change in specific **enthalpy** of the system:
|
|
|
|
|
|
|
|
$$c_p = \frac{\mathrm{d}q}{\mathrm{d}T} = \frac{\mathrm{d}h}{\mathrm{d}T}$$
|
|
|
|
|
|
|
|
</summary>
|
|
|
|
|
|
|
|
This is because given that pressure, $p$, is constant, work, $w$, can be expressed as:
|
|
|
|
|
|
|
|
$$w = -\int^2_1\! p \,\mathrm{d}v = -p(v_2 - v_1)$$
|
|
|
|
|
|
|
|
Applying the (1st corollary of the) 1st law to the closed system:
|
|
|
|
|
|
|
|
\begin{align*}
|
|
|
|
q + w &= u_2 - u_1 \rightarrow q = u_2 - u_1 + p(v_2 - v_1) \\
|
|
|
|
q &= u_2 + pv_2 - (u_1 + pv_1) \\
|
|
|
|
&= h_2 - h_1 = \mathrm{d}h \\
|
|
|
|
\therefore \mathrm{d}q &= \mathrm{d}h
|
|
|
|
\end{align*}
|
|
|
|
|
|
|
|
</details>
|
|
|
|
|
|
|
|
<details>
|
|
|
|
<summary>
|
|
|
|
|
|
|
|
#### Ratio of Specific Heats
|
|
|
|
|
|
|
|
$c_p > c_v$ is always true.
|
|
|
|
|
|
|
|
</summary>
|
|
|
|
|
|
|
|
Heating a volume of fluid, $V$, at a constant volume requires specific heat $q_v$ where
|
|
|
|
|
|
|
|
$$q_v = u_2 - u_1 \therefore c_v = \frac{q_v}{\Delta T}$$
|
|
|
|
|
|
|
|
Heating the same volume of fluid but under constant pressure requires a specific heat $q_p$ where
|
|
|
|
|
|
|
|
$$q_p =u_2 - u_1 + p(v_2-v_1) \therefore c_p = \frac{q_p}{\Delta T}$$
|
|
|
|
|
|
|
|
Since $p(v_2-v_1) > 0$, $\frac{q_p}{q_v} > 1 \therefore q_p > q_v \therefore c_p > c_v$.
|
|
|
|
|
|
|
|
The ratio $\frac{c_p}{c_v} = \gamma$
|
|
|
|
|
|
|
|
</details>
|
|
|
|
|
2021-12-23 17:28:35 +00:00
|
|
|
## Thermodynamic Processes and Cycles
|
|
|
|
|
2021-12-23 21:00:18 +00:00
|
|
|
When a thermodynamic system changes from one state to another it is said to execute a *process*.
|
2021-12-23 17:28:35 +00:00
|
|
|
An example of a process is expansion (volume increasing).
|
|
|
|
|
|
|
|
A *cycle* is a process or series of processes in which the end state is identical to the beginning.
|
|
|
|
And example of this could be expansion followed by a compression.
|
|
|
|
|
|
|
|
### Reversible and Irreversible Proccesses
|
|
|
|
|
|
|
|
During reversible processes, the system undergoes a continuous succession of equilibrium states.
|
|
|
|
Changes in the system can be defined and reversed to restore the intial conditions
|
|
|
|
|
|
|
|
All real processes are irreversible but some can be assumed to be reversible, such as controlled
|
|
|
|
expansion.
|
|
|
|
|
|
|
|
### Constant _____ Processes
|
|
|
|
|
|
|
|
#### Isothermal
|
|
|
|
|
|
|
|
Constant temperature process
|
|
|
|
|
|
|
|
#### Isobaric
|
|
|
|
|
|
|
|
Constant pressure process
|
|
|
|
|
|
|
|
#### Isometric / Isochoric
|
|
|
|
|
|
|
|
Constant volume process
|
|
|
|
|
|
|
|
## Heat and Work
|
|
|
|
|
|
|
|
Heat and Work are different forms of enery transfer.
|
|
|
|
|
|
|
|
They are both transient phenomena and systems never possess heat or work.
|
|
|
|
Both represent energy crossing boundaries when a system undergoes a change of state.
|
|
|
|
|
2021-12-23 21:00:18 +00:00
|
|
|
By convention, the transfer of energy into the system from the surroundings is positive (work is
|
|
|
|
being done *on* the system *by* the surroundings).
|
2021-12-23 17:28:35 +00:00
|
|
|
|
|
|
|
### Heat
|
|
|
|
|
|
|
|
*Heat* is defined as:
|
|
|
|
|
|
|
|
> The form of energy that is transferred across the boundary of a system at a given temperature to
|
|
|
|
> another system at a lower temperature by virtue of the temperature difference between the two
|
|
|
|
|
|
|
|
### Work
|
|
|
|
|
|
|
|
*Work* is defined as:
|
|
|
|
|
|
|
|
$$W = \int\! F \mathrm{d}x$$
|
|
|
|
|
|
|
|
(the work, $W$, done by a force, $F$, when the point of application of the force undergoes a
|
2021-12-23 21:00:18 +00:00
|
|
|
displacement, $\mathrm{d}x$)
|
|
|
|
|
|
|
|
## Thermally Insulated and Isolated Systems
|
|
|
|
|
|
|
|
In thermally insulated systems and isolated systems, heat transfer cannot take place.
|
|
|
|
|
|
|
|
In thermally isolated systems, work transfer cannot take place.
|
2021-12-23 17:28:35 +00:00
|
|
|
|
|
|
|
# Process and State Diagrams
|
|
|
|
|
|
|
|
Reversible processes are represented by solid lines, and irreversible processes by dashed lines.
|
2021-12-23 21:00:18 +00:00
|
|
|
|
|
|
|
# 1st Law of Thermodynamics
|
|
|
|
|
|
|
|
The 1st Law of Thermodynamics can be thought of as:
|
|
|
|
|
|
|
|
> When a closed system is taken through a cycle, the sum of the *net* work transfer ($W$) and *net*
|
|
|
|
> heat transfer ($Q$) equals zero:
|
|
|
|
>
|
|
|
|
> $$W_{net} + Q_{net} = 0$$
|
|
|
|
>
|
|
|
|
|
|
|
|
## 1st Corollary
|
|
|
|
|
|
|
|
> The change in internal energy of a closed system is equal to the sum of the heat transferred
|
|
|
|
> and the work done during any change of state
|
|
|
|
>
|
|
|
|
> $$W_{12} + Q_{12} = U_2 - U_1$$
|
|
|
|
|
|
|
|
## 2nd Corollary
|
|
|
|
|
|
|
|
> The internal energy of a closed system remains unchanged if it
|
|
|
|
> [thermally isolated](#thermally-insulated-and-isolated-systems) from its surroundings
|