The Otto Cycle

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The Otto cycle corresponds to an internal combustion engine in which heating occurs at a constant volume by turning on the mixture once the gas has been compressed.

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Mechanisms

Concept

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Carnot cycle

Concept

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Sadi Carnot introduced [1] the theoretical concept of the first machine design capable of generating mechanical work based on a heat gradient. This concept is realized through a process in the pressure-volume space where heat is added and extracted, as depicted in the image:



The area under curve the heat supplied ($Q_h$), spanning from 1 to 2, represents the energy input required to transition from state ($p_1, V_1$) to state ($p_2, V_2$). Conversely, the area under curve the absorbed heat ($Q_c$), going from 2 to 1, represents the energy extraction needed to return from state ($p_2, V_2$) back to state ($p_1, V_1$). The difference between these areas corresponds to the region enclosed by both curves and represents the work contributed or performed ($W$) that the system can perform.

Carnot also demonstrated that, in accordance with the second law of thermodynamics, the heat supplied ($Q_h$) cannot equal zero. This implies that no machine can convert all heat into work.

[1] "Réflexions sur la puissance motrice du feu et sur les machines propres à développer cette puissance" (Reflections on the Motive Power of Fire and on Machines Fitted to Develop That Power), Sadi Carnot, Annales scientifiques de lÉ.N.S. 2e série, tome 1, p. 393-457 (1872)

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Otto cycle: Pressure-volume diagram

Concept

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The Otto cycle [1] can be viewed as a technical solution based on the Carnot cycle. In this context, it consists of four stages:

• Stage 1 to 2: Adiabatic Compression $(p_1,V_1,T_1)\rightarrow(p_2,V_2,T_2)$,
• Stage 2 to 3: Heating $(p_2,V_2,T_2)\rightarrow(p_3,V_2,T_3)$,
• Stage 3 to 4: Adiabatic Expansion $(p_3,V_2,T_3)\rightarrow(p_4,V_1,T_4)$,
• Stage 4 to 1: Cooling $(p_4,V_1,T_4)\rightarrow(p_1,V_1,T_1)$

These stages are illustrated in the following diagram:



In the diagram, the energy flow is illustrated, where the heat supplied ($Q_h$) adds energy, raising the temperature from the temperature in state 2 ($T_2$) to the temperature in state 3 ($T_3$). It enters the system and performs ($$) units of work, while the counterpart the absorbed heat ($Q_c$) is absorbed, lowering the temperature from the temperature in state 4 ($T_4$) to the temperature in state 1 ($T_1$).

[1] "Verbrennungsmotor" (Internal combustion engine), N. A. Otto, Kaiserlichen Patentamts, Patent 532, January 2, 1877

Note: In 1862, Nikolaus Otto attempted to construct the internal combustion engine patented by Alphonse Beau de Rochas without success. He later modified it and succeeded in building a functional one in 1877, manufacturing 30,000 silent and highly reliable engines. He patented his design in 1877; however, the patent was later revoked due to the existence of Alphonse Beau de Rochas' patent, even though Rochas never managed to build his version. Since Otto was the first to make the engine work, his version is remembered today, labeling the process the "Otto Cycle."

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Technical Solution

Image

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The Otto engine operates in two cycles: the actual Otto cycle, which consists of the following phases:

• Phase 1 to 2: Adiabatic compression
• Phase 2 to 3: Heating
• Phase 3 to 4: Adiabatic expansion
• Phase 4 to 1: Cooling

In addition, it has a cycle for emptying the burnt gases and filling with a fresh mixture.



For this reason, it is referred to as a two-stroke engine. The emptying and filling phase can be accomplished using a compensating mass or through a second cylinder that operates out of phase.

The efficiency the efficiency ($\eta$) of the engine can be estimated using the otto compressibility factor ($r$) and the adiabatic index ($\kappa$) with the following equation:

$ \eta = 1-\displaystyle\frac{1}{ r ^{ \kappa -1}}$

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Model

Concept

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Adiabatic compression

Equation

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Given that in an adiabatic expansion, the gas satisfies the relationship with the volume in state i ($V_i$), the volume in state f ($V_f$), the temperature in initial state ($T_i$), and the temperature in final state ($T_f$):

$ T_i V_i ^{ \kappa -1}= T_f V_f ^{ \kappa -1}$



In this case, from the initial point 1 to point 2. This means that during the adiabatic compression, the state of the gas changes from the expanded volume ($V_1$) and the temperature in state 1 ($T_1$) to the compressed volume ($V_2$) and the temperature in state 2 ($T_2$) as follows:

$ T_1 V_1 ^{ \kappa - 1} = T_2 V_2 ^{ \kappa - 1}$

$\kappa$
Adiabatic index
$-$
$V_2$
Compressed volume
$m^3$
$V_1$
Expanded volume
$m^3$
$T_1$
Temperature in state 1
$K$
$T_2$
Temperature in state 2
$K$

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Heat supplied

Equation

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When supplying the heat supplied ($Q_h$), the temperature of the gas increases from $T_2$ to $T_3$ in an isochoric process (at constant volume). This implies that we can utilize the relationship for ($$) with the heat capacity at constant volume ($C_V$) and the variación de Temperature ($\Delta T$), expressed by the equation:

$ \Delta Q = C_V \Delta T $



This results in the temperature in state 2 ($T_2$) and the temperature in state 3 ($T_3$) as follows:

$ Q_h = C_V ( T_3 - T_2 )$

$C_V$
Heat capacity at constant volume
$J/K$
$Q_H$
Heat supplied
$J/mol$
$T_2$
Temperature in state 2
$K$
$T_3$
Temperature in state 3
$K$

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Adiabatic expansion

Equation

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Given that in an adiabatic expansion the gas satisfies the equation

$ T_i V_i ^{ \kappa -1}= T_f V_f ^{ \kappa -1}$

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we can conclude that in the state transition from ($V_2,T_3$) to ($V_1,T_4$), the following relationship holds:

$ T_4 V_1 ^{ \kappa - 1} = T_3 V_2 ^{ \kappa - 1}$

$\kappa$
Adiabatic index
$-$
$V_2$
Compressed volume
$m^3$
$V_1$
Expanded volume
$m^3$
$T_3$
Temperature in state 3
$K$
$T_4$
Temperature in state 4
$K$

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Heat removed

Equation

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When removing the heat $Q_c$, the temperature of the gas decreases from $T_4$ to $T_1$ in an isochoric process (constant volume), which means that we can use the equation:

$ \Delta Q = C_V \Delta T $



As a result of this equation, we have:

$ Q_c = C_V ( T_4 - T_1 )$

$Q_c$
Absorbed heat
$J$
$C_V$
Heat capacity at constant volume
$J/K$
$T_1$
Temperature in state 1
$K$
$T_4$
Temperature in state 4
$K$

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Efficiency as a function of temperatures

Equation

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The efficiency ($\eta$) for the Otto cycle case can be calculated from the expression involving the absorbed heat ($Q_c$) and the heat supplied ($Q_h$):

$ \eta = 1-\displaystyle\frac{ Q_c }{ Q_h } $



If we substitute the heat values with their expressions in terms of the temperature in state 1 ($T_1$), the temperature in state 2 ($T_2$), the temperature in state 3 ($T_3$), and the temperature in state 4 ($T_4$):

$ \eta =1-\displaystyle\frac{ T_4 - T_1 }{ T_3 - T_2 }$

$\eta$
Efficiency
$-$
$T_1$
Temperature in state 1
$K$
$T_2$
Temperature in state 2
$K$
$T_3$
Temperature in state 3
$K$
$T_4$
Temperature in state 4
$K$

The absorbed heat ($Q_c$) is related to the heat capacity at constant volume ($C_V$), the temperature in state 4 ($T_4$), and the temperature in state 1 ($T_1$) according to the following equation:

$ Q_c = C_V ( T_4 - T_1 )$



And the heat supplied ($Q_h$) is related to the heat capacity at constant volume ($C_V$), the temperature in state 3 ($T_3$), and the temperature in state 2 ($T_2$) through the equation:

$ Q_h = C_V ( T_3 - T_2 )$



Therefore, in the equation for the efficiency ($\eta$) represented by:

$ \eta = 1-\displaystyle\frac{ Q_c }{ Q_h } $



We have the following relationship:

$ \eta =1-\displaystyle\frac{ T_4 - T_1 }{ T_3 - T_2 }$

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Compressibility factor $r$

Equation

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The efficiency ($\eta$) is ultimately a function of the expanded volume ($V_1$) and the compressed volume ($V_2$), and in particular, of the otto compressibility factor ($r$):

$ r =\displaystyle\frac{ V_1 }{ V_2 }$

$V_2$
Compressed volume
$m^3$
$V_1$
Expanded volume
$m^3$
$r$
Otto compressibility factor
$-$

Adiabatic expansion is described using the variables the adiabatic index ($\kappa$), the temperature in state 4 ($T_4$), the temperature in state 3 ($T_3$), the expanded volume ($V_1$), and the compressed volume ($V_2$) through the relationship

$ T_4 V_1 ^{ \kappa - 1} = T_3 V_2 ^{ \kappa - 1}$



While adiabatic compression is represented by the temperature in state 1 ($T_1$) and the temperature in state 2 ($T_2$) through the relationship

$ T_1 V_1 ^{ \kappa - 1} = T_2 V_2 ^{ \kappa - 1}$



By subtracting the second equation from the first, we obtain

$(T_4 - T_1)V_1^{\kappa-1} = (T_3 - T_2)V_2^{\kappa-1}$



Which leads us to the relationship

$\left(\displaystyle\frac{V_1}{V_2}\right)^{\kappa-1} = \displaystyle\frac{T_3 - T_2}{T_4 - T_1}$



And this allows us to define the otto compressibility factor ($r$) as follows:

$ r =\displaystyle\frac{ V_1 }{ V_2 }$

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Efficiency depending on the compressibility factor

Equation

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The efficiency ($\eta$) can be defined in terms of the temperature in state 1 ($T_1$), the temperature in state 2 ($T_2$), the temperature in state 3 ($T_3$), and the temperature in state 4 ($T_4$) in the process, as per the equation:

$ \eta =1-\displaystyle\frac{ T_4 - T_1 }{ T_3 - T_2 }$



However, temperatures are related to volumes through the gas equations. Therefore, it is possible to reformulate efficiency in terms of the otto compressibility factor ($r$), which represents the ratio between the expanded volume and the compressed volume. In this way, using the adiabatic index ($\kappa$), we obtain the efficiency of a process using the Otto cycle:

$ \eta = 1-\displaystyle\frac{1}{ r ^{ \kappa -1}}$

$\kappa$
Adiabatic index
$-$
$\eta$
Efficiency
$-$
$r$
Otto compressibility factor
$-$

The efficiency ($\eta$), in terms of the temperature in state 1 ($T_1$), the temperature in state 2 ($T_2$), the temperature in state 3 ($T_3$), and the temperature in state 4 ($T_4$), is calculated using the equation:

$ \eta =1-\displaystyle\frac{ T_4 - T_1 }{ T_3 - T_2 }$



In the case of adiabatic expansion, it is described using the adiabatic index ($\kappa$), the expanded volume ($V_1$), and the compressed volume ($V_2$) with the relationship:

$ T_4 V_1 ^{ \kappa - 1} = T_3 V_2 ^{ \kappa - 1}$



And adiabatic compression is represented by the relationship:

$ T_1 V_1 ^{ \kappa - 1} = T_2 V_2 ^{ \kappa - 1}$



If we subtract the second equation from the first, we obtain:

$(T_4 - T_1)V_1^{\kappa-1} = (T_3 - T_2)V_2^{\kappa-1}$



Which leads to the relationship:

$\left(\displaystyle\frac{V_1}{V_2}\right)^{\kappa-1} = \displaystyle\frac{T_3 - T_2}{T_4 - T_1}$



This, in turn, leads to the definition of the otto compressibility factor ($r$) with the equation:

$ r =\displaystyle\frac{ V_1 }{ V_2 }$



With all these components, the efficiency of a process using the Otto cycle can be calculated as:

$ \eta = 1-\displaystyle\frac{1}{ r ^{ \kappa -1}}$

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