By securing stakeholder needs throughout the project planning stage via thorough process documentation that is revised after each work cycle.
Answer:
T2 ( final temperature ) = 576.9 K
a) 853.4 kJ/kg
b) 1422.3 kJ / kg
Explanation:
given data:
pressure ( P1 ) = 90 kPa
Temperature ( T1 ) = 30°c + 273 = 303 k
P2 = 450 kPa
To determine final temperature in an Isentropic process
----------- ( 1 )
T2 = 303
= 576.9K
The work performed in a piston-cylinder device is calculated using the subsequent formula
------- ( 2 )
where: cv = 3.1156 kJ/kg.k for helium gas
T2 = 576.9K, T1 = 303 K
substituting values into equation 2
= 853.4 kJ/kg
the work done in a steady flow compressor is determined using this

where: cp ( constant pressure of helium gas ) = 5.1926 kJ/kg.K
T2 = 576.9 k, T1 = 303 K
plugging values back into equation 3
= 1422.3 kJ / kg
Explanation:
At a temperature of
and relative humidity of 86%, the humidity ratio stands at 0.0223 with a specific volume of 14.289.
At a temperature of
and relative humidity of 40%, the humidity ratio is 0.0066 while the specific volume is 13.535.
To determine the mass of air, the following formula can be used:

Now, we will calculate the volume

The duration required to fill the cistern can be determined with the equation:

By substituting the values into the preceding formula, we find:

Thus, the hours necessary to fill the cistern amount to 4.65 hours.
Answer:
Explanation:
In a steady-state condition, the total volume exiting matches the total volume entering, and
the total amount of salt entering equals the total amount of salt exiting.
The volume entering each minute is = 2000 + 2 x 10³ x 60
= 122000 L.
The total salt entering per minute = 1200 x 2000 + 20 x 2 x 10³ x 60
= 2400000 + 2400000 mg
= 4800000 mg.
The volume of water exiting each minute = 122000 L.
The total salt exiting each minute = 4800000 mg.
The concentration of salt in the exiting water = 4800000 / 122000
= 39.344 mg / L.