Act like a helpful tutor and exlain me :
Give step-by-step solution with explanation and final answer:solve all parts completely , Nitrogen, modeled as an ideal gas, flows at a rate of
3
k
g
s
through a well
-
insulated horizontal nozzle operating at steady state. The nitrogen enters the nozzle with a velocity of
2
0
m
s
at
5
0
0
K
,
4
0
0
kPa and exits the nozzle at
1
0
0
kPa
.
To achieve an exit velocity of
3
0
0
m
s
,
determine:
(
a
)
the exit temperature, in K
.
(
b
)
the exit area,
i
n
2
.
Question:
Act like a helpful tutor and exlain me :
Give step-by-step solution with explanation and final answer:solve all parts completely , Nitrogen, modeled as an ideal gas, flows at a rate of
3
k
g
s
through a well
-
insulated horizontal nozzle operating at steady state. The nitrogen enters the nozzle with a velocity of
2
0
m
s
at
5
0
0
K
,
4
0
0
kPa and exits the nozzle at
1
0
0
kPa
.
To achieve an exit velocity of
3
0
0
m
s
,
determine:
(
a
)
the exit temperature, in K
.
(
b
)
the exit area,
i
n
2
.
This is AI generated Response.
Asked by: manish kumar
Created at: 2025-10-08 09:02:09
Final Answer:
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# Nitrogen No Problem (Ideal)
We are:
- **Mass flow rate:**(\dot{m} = 3\, \text{kg/s}\)
-Inlet velocity:** \(V_1 = 20\, \text{m/s}\)
- **Inlet temperature:** \(T_1 = 500\, \text{K}\)
- **Inlet pressure:** \(P_1 = 400\, \text{kPa}\)
- **Exit pressure:** \(P_2 = 100\, \text{kPa}\)
- **Exit velocity:** \(V_2 = 300\, \text{m/s}\)
- **Nitrogen is an ideal gas.**
We need to find:
- (a) **Exit temperature, \(T_2\) (in K)**
- (b) **Exit area, \(A_2\) (in m²)**
---
## Step 1: Apply the Steady-Flow Energy Equation (SFEE)
Since the nozzle is horizontal and well-insulated (adiabatic), the SFEE simplifies to:
\[
h_1 + \frac{V_1^2}{2} = h_2 + \frac{V_2^2}{2}
\]
Where \(h\) is specific enthalpy.
For an ideal gas:
\[
h = c_p T
\]
The specific heat at constant pressure for nitrogen (\(N_2\)) is approximately:
\[
c_p = 1.039\, \text{kJ/kg}\cdot\text{K} = 1039\, \text{J/kg}\cdot\text{K}
\]
---
## (a) Find the Exit Temperature \(T_2\)
Plug in values (keep units consistent):
\[
c_p T_1 + \frac{V_1^2}{2} = c_p T_2 + \frac{V_2^2}{2}
\]
\[
T_2 = T_1 + \frac{V_1^2 - V_2^2}{2 c_p}
\]
Plug in the numbers:
- \(T_1 = 500\, \text{K}\)
- \(V_1 = 20\, \text{m/s}\)
- \(V_2 = 300\, \text{m/s}\)
- \(c_p = 1039\, \text{J/kg}\cdot\text{K}\)
Calculate:
\[
T_2 = 500 + \frac{20^2 - 300^2}{2 \times 1039}
\]
\[
T_2 = 500 + \frac{400 - 90000}{2078}
\]
\[
T_2 = 500 + \frac{-89600}{2078}
\]
\[
T_2 = 500 - 43.11
\]
\[
T_2 \approx 456.9\, \text{K}
\]
**Final answer (a):**
\[
\boxed{T_2 \approx 457\, \text{K}}
\]
---
## (b) Find the Exit Area \(A_2\)
Use the mass flow rate relationship:
\[
\dot{m} = \rho_2 V_2 A_2
\]
First, find \(\rho_2\) (density at exit):
Ideal gas law:
\[
\rho_2 = \frac{P_2}{R T_2}
\]
Where \(R\) for nitrogen, \(R = \frac{R_u}{M}\):
- \(R_u = 8314\, \text{J/kmol}\cdot\text{K}\)
- \(M = 28.013\, \text{kg/kmol}\)
So,
\[
R = \frac{8314}{28.013} \approx 297.1\, \text{J/kg}\cdot\text{K}
\]
Plug in values:
- \(P_2 = 100\, \text{kPa} = 100,000\, \text{Pa}\)
- \(T_2 \approx 457\, \text{K}\)
\[
\rho_2 = \frac{100{,}000}{297.1 \times 457}
\]
\[
\rho_2 \approx \frac{100{,}000}{135,794}
\]
\[
\rho_2 \approx .736\, \text{kg/m}^3
\]
Now, rearrange for \(A_2\):
\[
A_2 = \frac{\dot{m}}{\rho_2 V_2}
\]
\[
A_2 = \frac{3}{.736 \times 300}
\]
\[
A_2 = \frac{3}{220.8}
\]
\[
A_2 \approx .0136\, \text{m}^2
\]
**Final answer (b):**
\[
\boxed{A_2 \approx .0136\, \text{m}^2}
\]
---
## **Summary of Answers**
- **(a) Exit temperature:** \(\boxed{457\, \text{K}}\)
- **(b) Exit area:** \(\boxed{.0136\, \text{m}^2}\)
---
**Note:**
- Calculations use rounded values for readability.
- For more precision, carry more significant digits through calculations.
- Assumed \(c_p\) and \(R\) for nitrogen are constant in this temperature range; for more accurate results, use property tables.
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