Act like a helpful tutor and exlain me : Give step-by-step solution with explanation and final answer: inlet diameter is not givencesgeis FeoosRiy gEEcisd ESESRES © giilEce d3fgesd LER 1 Ii i Hi | Eg gi i ~38 SI i op:
Question:
Act like a helpful tutor and exlain me :
Give step-by-step solution with explanation and final answer:
inlet diameter is not givencesgeis
FeoosRiy
gEEcisd
ESESRES
© giilEce
d3fgesd
LER 1
Ii
i Hi
|
Eg
gi i
~38
SI
i op:
This is AI generated Response.
Asked by: manish kumar
Created at: 2025-10-11 08:49:39
Asked by: manish kumar
Created at: 2025-10-11 08:49:39
Final Answer:
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Let's break down the question step by step:
---
## **Question Recap**
- **Water flow rate**: \( Q = .130 \, \text{kg/s} \) *(mass flow rate)*
- **Inlet velocity**: \( v_1 = 1.5 \, \text{m/s} \)
- **Outlet velocity**: \( v_2 = 15 \, \text{m/s} \)
- **Gauge pressure at outlet**: \( P_2 = 15 \, \text{psi} = 103.4 \, \text{kPa} \) *(1 psi = 6.895 kPa)*
- **Correction factor**: \( \beta = .94 \)
- **Density of water**: \( \rho = 100 \, \text{kg/m}^3 \)
- **Neglect elevation and weight of hose**
Let's answer each part step by step.
---
## **(a) Calculate the Inlet Area**
We know:
\[
Q = \dot{m} = \rho \cdot A_1 \cdot v_1
\]
\[
A_1 = \frac{\dot{m}}{\rho v_1}
\]
Where:
- \( \dot{m} = .130\, \text{kg/s} \)
- \( \rho = 100\, \text{kg/m}^3 \)
- \( v_1 = 1.5\, \text{m/s} \)
Plug in the values:
\[
A_1 = \frac{.130}{100 \times 1.5}
= \frac{.130}{150}
= 8.67 \times 10^{-5} \, \text{m}^2
\]
---
## **(b) Calculate the Gauge Pressure at the Hose Inlet**
Apply the **steady-flow energy (Bernoulli) equation** between inlet (1) and outlet (2):
\[
\frac{P_1}{\rho} + \frac{v_1^2}{2} = \frac{P_2}{\rho} + \frac{v_2^2}{2}
\]
(Since elevation head and velocity correction factors are negligible/absent.)
Solve for \( P_1 \):
\[
P_1 = P_2 + \frac{\rho}{2}(v_2^2 - v_1^2)
\]
Given:
- \( P_2 = 103,425 \, \text{Pa} \)
- \( v_2 = 15 \, \text{m/s} \)
- \( v_1 = 1.5 \, \text{m/s} \)
- \( \rho = 100 \, \text{kg/m}^3 \)
\[
P_1 = 103,425 + \frac{100}{2} (15^2 - 1.5^2)
= 103,425 + 500 (225 - 2.25)
= 103,425 + 500 \times 222.75
= 103,425 + 111,375
= 214,800 \, \text{Pa}
\]
\[
\boxed{P_1 = 214.8 \, \text{kPa}}
\]
---
## **(c) Calculate the Anchoring Force (Magnitude and Direction)**
Use **momentum equation** for a control volume:
\[
\sum F_x = \dot{m} (v_{2x} - v_{1x})
\]
Where:
- \(\sum F_x\) = net force acting on the control volume (hose)
- \(v_{2x}\) and \(v_{1x}\) = velocities at outlet and inlet
Forces acting (in x-direction):
1. Pressure at inlet (\(P_1 A_1\), acts right)
2. Pressure at outlet (\(P_2 A_2\), acts left)
3. Anchoring force (\(F\), acts left)
So,
\[
F + P_2 A_2 - P_1 A_1 = \dot{m}(v_2 - v_1)
\]
\[
F = \dot{m}(v_2 - v_1) + P_1 A_1 - P_2 A_2
\]
Calculate \(A_2\):
\[
Q = \dot{m}/\rho = A_2 v_2 \implies A_2 = \frac{\dot{m}}{\rho v_2}
= \frac{.130}{100 \times 15}
= \frac{.130}{15,000}
= 8.67 \times 10^{-6} \, \text{m}^2
\]
Now, plug in:
- \(\dot{m} = .130\, \text{kg/s}\)
- \(v_2 - v_1 = 15 - 1.5 = 13.5\, \text{m/s}\)
- \(P_1 = 214,800\, \text{Pa}\)
- \(A_1 = 8.67 \times 10^{-5}\, \text{m}^2\)
- \(P_2 = 103,425\, \text{Pa}\)
- \(A_2 = 8.67 \times 10^{-6}\, \text{m}^2\)
\[
F = (.130 \times 13.5) + (214,800 \times 8.67 \times 10^{-5}) - (103,425 \times 8.67 \times 10^{-6})
\]
\[
F = 1.755 + 18.62 - .897
\]
\[
F = 1.755 + 18.62 - .897 = 19.478\, \text{N}
\]
**Direction:** The force acts **to the left** (to hold the hose in place).
---
## **Summary of Answers**
**(a) Inlet area:**
\[
\boxed{A_1 = 8.67 \times 10^{-5} \, \text{m}^2}
\]
**(b) Gauge pressure at inlet:**
\[
\boxed{P_1 = 214.8 \, \text{kPa}}
\]
**(c) Anchoring force (magnitude and direction):**
\[
\boxed{19.5 \, \text{N}, \text{ to the left}}
\]
---
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