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Nady [450]
3 years ago
10

Argon is compressed in a polytropic process with = 1:3 (i.e., PV = costant) from 120 kPa and 10 C until it reaches a temperature

of 120 C in a piston{cylinder device. Model the system as an ideal gas and determine the speci c work (work per unit mass) done by the gas and the heat per unit mass transferred during this the process.
Engineering
1 answer:
Luden [163]3 years ago
6 0

Answer:

The work done per unit kg of mass is -76.08 kJ/kg while the heat transferred per unit kg of mass is -42.01 kJ/kg.

Explanation:

For Argon the molar mass is given as

M=40

Now the gas constant for Argon is given as

R=\frac{\bar{R}}{M}\\R=\frac{8.314}{40}\\R=0.208 kJ/K kg

Initial Temperature is T_1=10 C=10+273=283 K

Final Temperature is T_2=120 C=120+273=393 K

Initial Pressure is P_1=120 kPa

The initial volume is given as

v_1=\frac{RT_1}{P_1}\\v_1=\frac{0.208\times 283}{120}\\v_1=0.491 m^3/kg

For the polytropic process with γ=1.3 is given as

             \frac{P_2}{P_1}=(\frac{T_2}{T_1})^{\frac{\gamma}{\gamma-1}}\\\frac{P_2}{120}=(\frac{393}{283})^{\frac{1.3}{1.3-1}}\\\frac{P_2}{120}=(\frac{393}{283})^{\frac{1.3}{0.3}}\\\frac{P_2}{120}=(\frac{393}{283})^{\frac{1.3}{0.3}}\\{P_2}=(\frac{393}{283})^{\frac{1.3}{0.3} }\times 120\\P_2=497.9 kPA

Now the volume at the second stage is given as

               v_2=\frac{RT_2}{P_2}\\v_2=\frac{0.208\times 393}{497.9}\\v_2=0.164 m^3/kg

Now the work done per kg mass is given as

w=\frac{p_1v_1-p_2v_2}{\gamma-1}\\w=\frac{120\times 0.491-497.9 \times 0.164}{1.3-1}\\w=-76.08 kJ/kg

So the work done per unit kg of mass is -76.08 kJ/kg.

The heat per unit mass is given as

Q_{poly}=\frac{\gamma_{adi}-\gamma_{poly}}{\gamma_{adi}-1} \times w_{poly}

As the Argon gas is monotonic which gives γ_adiabatic=1.67

Q_{poly}=\frac{\gamma_{adi}-\gamma_{poly}}{\gamma_{adi}-1} \times w_{poly}\\Q_{poly}=\frac{1.67-1.3}{1.67-1} \times (-76.08 kJ/kg)\\Q_{poly}=-42.01 kJ/kg

The heat transferred per unit kg of mass is -42.01 kJ/kg

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Vsevolod [243]

Answer:

a) Please see attached copy below

b) 0.39KJ

c)  20.9‰

Explanation:

The three process of an air-standard cycle are described.

Assumptions

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2. Kinetic and potential energy negligible.

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b) T₁=290K ⇒ u₁=206.91 kj/kg, h₁=290.16 kj/kg.

P₂V₂/T₂=P₁V₁/T₁⇒ T₂=P₂T₁/P₁ = 380/95(290K)= 1160K

T₃=T₂(P₃/P₂)⁽k₋1⁾/k =(1160K)(95/380)⁽⁰°⁴/₁.₄⁾ =780.6K

Qin=m(u₂₋u₁)=mCv(T₂-T₁)

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Qout=m(h₃₋h₁)=mCp(T₃₋T₁)

=0.003KG×(1.005kj/kg.k(780.6-290)K= 1.48KJ

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Answer:

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4.Constant volume heat rejection

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5 0
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grin007 [14]

Answer:

835,175.68W

Explanation:

Calculation to determine the required power input to the pump

First step is to calculate the power needed

Using this formula

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Where,

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p represent brine density=1050 kg/m³

g represent gravity=9.81m/s²

h represent height=200m

Let plug in the formula

P=0.3 m³/s *1050 kg/m³*9.81m/s² *200m

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Now let calculate the required power input to the pump

Using this formula

Required power input=P/μ

Where,

P represent power=618,030 W

μ represent pump efficiency=74%

Let plug in the formula

Required power input=618,030W/0.74

Required power input=835,175.68W

Therefore the required power input to the pump will be 835,175.68W

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