Answer:

Part A:
(-ve sign shows heat is getting out)
Part B:
(Heat getting in)
The value of Q at constant specific heat is approximately 361% in difference with variable specific heat and at constant specific heat Q has opposite direction (going in) than Q which is calculated in Part B from table A-23. So taking constant specific heat is not a good idea and is questionable.
Explanation:
Assumptions:
- Gas is ideal
- System is closed system.
- K.E and P.E is neglected
- Process is polytropic
Since Process is polytropic so 
Where n=1.25
Since Process is polytropic :


Now,


We will now calculate mass (m) and Temperature T_2.


Part A:
According to energy balance::

From A-20, C_v for Carbon dioxide at 300 K is 0.657 KJ/Kg.k

(-ve sign shows heat is getting out)
Part B:
From Table A-23:

(By interpolation)


(Heat getting in)
The value of Q at constant specific heat is approximately 361% in difference with variable specific heat and at constant specific heat Q has opposite direction (going in) than Q which is calculated in Part B from table A-23. So taking constant specific heat is not a good idea and is questionable.
Answer:
x = 3.92
Explanation:
The question is given as ;
40 = 6x² / 4 tan { 180/6}
40 = 6x² / 4 tan {30°}
40 = 6x² / 2.309
40 * 2.309 = 6x²
92.38 = 6 x²
92.38/6 = x²
15.40 = x²
√15.40 = x
x = 3.92
Answer:
The question is not complete. So, I try to find the complete question & complete answer of the question is given in attached file.
Explanation:
Answer:
lol contrates brother......
Answer:


Explanation:
given data:
Diameter =





from continuity equation



![v_2 = [\frac{d_1}{d_2}]^2 v_1](https://tex.z-dn.net/?f=v_2%20%3D%20%5B%5Cfrac%7Bd_1%7D%7Bd_2%7D%5D%5E2%20v_1)
![= [\frac{0.200}{0.158}]^2 \times 100](https://tex.z-dn.net/?f=%3D%20%5B%5Cfrac%7B0.200%7D%7B0.158%7D%5D%5E2%20%5Ctimes%20100)

by energy flow equation

and q =0, w =0 for nozzle
therefore we have


but we know dh = Cp dt
hence our equation become




