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Oxygen (O2) at 25C,\left(\mathrm{O}_{2}\right) \text { at } 25^{\circ} \mathrm{C}, 100 kPa enters a compressor operating at steady state and exits at 260C,260^\circ C, 650 kPa. Stray heat transfer and kinetic and potential energy effects are negligible. Modeling the oxygen as an ideal gas with k = 1.379, determine the isentropic compressor efficiency and the work in kJ per kg of oxygen flowing.

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Given\text{\textcolor{#4257b2}{\textbf{Given}}}

Temperature at state 1 T1=25 CT_1=25 \ \mathrm{^\circ C}

Temperature at state 2 T2=260 CT_2=260 \ \mathrm{^\circ C}

Pressure at state 1 P1=100 KPaP_1=100 \ \mathrm{KPa}

Pressure at state 2 P2=650 KPaP_2=650 \ \mathrm{KPa}

Specific heat constant of oxygen K=1.379K = 1.379

Required\text{\textcolor{#4257b2}{\textbf{Required}}}

The work developed [KJKg]\left[ \mathrm{\dfrac{KJ}{Kg}} \right]

The isentropic compressor efficiency.

Assumption\text{\textcolor{#4257b2}{\textbf{Assumption}}}

Oxygen in a compressor assembly is compressed adiabatically .

The steam is a closed system.

Applying the ideal gas model.

Kinetic energy play can be neglected.

Potential energy play can be neglected.

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