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mel-nik [20]
3 years ago
8

Steam at 150 bars and 600°C passes through process equipment and emerges at 100 bars and 700°C. There is no flow of work into or

out of the equipment, but heat is transferred. a. Compute the flow of heat into the process equipment per kg of steam.b. Compute the value of enthalpy at the inlet conditions.Consider steam at 1 bar and 600°C as an ideal gas. Express your answer as (Hin – Hig)/RTin
Engineering
1 answer:
Goshia [24]3 years ago
6 0

Answer:

a) q_in = 286.9 KJ/kg

b) H_ig = 1918.9413 KJ/kg ,  (Hin – Hig)/RTin = 4.43

Explanation:

Given:

State 1: Steam @

  - P_1 = 150 bars

  - T_1 = 600 C

State 1: Steam @

  - P_2 = 100 bars

  - T_1 = 700 C

- No work done W_net = 0

Find:

- q_in

- Compare h_1 from property table with h_1 with ideal gas steam @P = 1 bar and T = 600 C.

Solution:

State 1:

Use Table A-5

h_1 = 3583.1 KJ/kg

State 2:

Use Table A-5

h_2 = 3870 KJ/kg

- The Thermodynamic balance is as follows:

                                q_in - w = h_2 - h_1

                                q_in = h_2 - h_1

                                q_in = 3870 - 3583.1 = 286.9 KJ/kg

- Enthalpy H_ig of ideal gas @P = 1 bar and T_in = 600 C

                                c_p = 2.1981 KJ / kg.K         @ T_in = 600 + 273 = 873 K

                                H_ig = c_p*T_in

                                H_ig = 2.1981*873 = 1918.9413 KJ/kg

- Enthalpy H_in of steam @P = 1 bar and T_in = 600 C

  Using Table A-5

  H_in = 3705.6 KJ/kg

- Relative Enthalpy:

                               (Hin – Hig)/RTin = (3705.6 - 1918.9413) / 0.462*873

                               (Hin – Hig)/RTin = 4.43

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A thin plastic membrane is used to separate helium from a gas stream. Under steady-state conditions the concentration of helium
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5 0
3 years ago
A pump is used to extract water from a reservoir and deliver it to another reservoir whose free surface elevation is 200 ft abov
babunello [35]

Answer:

a) the expected flow rate is 31.4 ft³/s

b) the required brake horsepower is 2808.4 bhp

c) the location of pump inlet to avoid cavitation is -8.4 ft

Explanation:

Given the data in the question;

free surface elevation = 200 ft

total length of pipe required = 1000 ft

diameter = 12 inch

Iron with relative roughness ( k/D ) = 0.0005

H_{pump = 665-0.051Q² [Qinft ]

a) the expected flow rate

given that;

k/D  = 0.0005

k/2R = 0.0005

R/k = 1000

now, we determine the friction factor;

1/√f = 2log₁₀( R/k ) + 1.74

we substitute

1/√f = 2log₁₀( 1000 ) + 1.74

1/√f = 6 + 1.74

1/√f = 7.74

√f = 1/7.74

√f = 0.1291989

f = (0.1291989)²

f = 0.01669

Now, Using Bernoulli theorem between two reservoirs;

(p/ρq)₁ + (v²/2g)₁ + z₁ + H_p = (p/ρq)₂ + (v²/2g)₂ + z₂ + h_L

so

0 + 0 + 0 + 665-0.051Q² = 0 + 0 + 200 + flQ²/2gdA²

665-0.051Q² = 200 + flQ²/2gdA²

665-0.051Q² = 200 +[  ( 0.01669 × 1000 × Q² ) / (2 × 32.2 × (π/4)² × 1⁵ )

665 - 0.051Q² = 200 + [ 16.69Q² / 39.725 ]

665 - 200 - 0.051Q² = 0.420138Q²

665 - 200 = 0.420138Q² + 0.051Q²

465 = 0.471138Q²

Q² = 465 / 0.471138

Q² = 986.97196

Q = √986.97196

Q = 31.4 ft³/s

Therefore, the expected flow rate is 31.4 ft³/s

b) the brake horsepower required to drive the pump (assume an efficiency of 78%).

we know that;

P = ρgH_pQ / η

where; H_p = 665 - 0.051(986.97196) = 614.7

we substitute;

P = ( 62.42 × 614.7 × 31.4 ) / ( 0.78 × 550 )

P = 1204804.6236 / 429

P = 2808.4 bhp

Therefore, the required brake horsepower is 2808.4 bhp

c) the location of pump inlet to avoid cavitation (assume the required NPSH=25 ft).

NPSH = (P_{atom / ρg) - h_s - ( P_v / ρg )

we substitute

25  = ( 2116 / 62.42 ) - h_s - ( 30 / 62.42 )

h_s = 8.4 ft

Therefore, the location of pump inlet to avoid cavitation is -8.4 ft

6 0
3 years ago
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