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Roll No. HEEEEEEE [ ] Total No. of Pages : 02
Total No. of Questions : 09
B.Tech.(Petroleum Refinary Engineering) (2013 Batch) (Sem.-4)
CHEMICAL ENGINEERING THERMODYNAMICS
Subject Code : BTPC-404/BTCH-305
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M.Code : 72427
Time : 3 Hrs. Max. Marks : 60
INSTRUCTIONS TO CANDIDATES :
- SECTION-A is COMPULSORY consisting of TEN questions carrying TWO marks each.
- SECTION-B contains FIVE questions carrying FIVE marks each and students have to attempt any FOUR questions.
- SECTION-C contains THREE questions carrying TEN marks each and students have to attempt any TWO questions.
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SECTION-A
- Answer briefly :
- Write the van der Waals equation of state for 5 moles of gas.
- State 3rd law of thermodynamics. What is its significance?
- What is throttling process? Give an example.
- What is the significance of mollier- diagram?
- What do you understand by fugacity and activity?
- What is chemical potential? What is its significance?
- What are the criteria of chemical reaction equilibrium?
- What is the effect of pressure on equilibrium constant in a gas phase reaction?
- Write two major applications of Gibb’s Duhem equation.
- What is the physical significance of partial molar volume?
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SECTION-B
- Calculate the change in internal energy, change in enthalpy, work done and the heat supplied in process when an ideal gas is expanded from 5 bar to 4 bar isothermally at 600 K.
- Describe Linde’s cycle of liquefaction of gases.
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- Prove that the efficiency of Carnot's cycle depends only upon two extreme temperatures in which the engine works.
- An ideal gas is compressed adiabatically from 1.5 bar, 338 K to 9 bar. The process is reversible and y = 1.23 is constant over the entire range of conditions.
Calculate :- The temperature at the end of compression.
- The work of compression.
- If the partial molar volumes of species 1 in a binary liquid solution at constant temperature and pressure is given by V1 =V1 +ax22; derive the equation for V2 .
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SECTION-C
- Derive an expression for fugacity coefficient of a gas obeying the equation of state V =a+bP+cP2, where P is in bar. Determine fugacity of oxygen at 293 K and 100 bar, given that a = 1.0; b= -0.753 x 10-3 and c = 0.15 x 10-7.
- The enthalpy at 300 K and 1 bar of a binary liquid mixture is
H =400 x1 + 600 x2 + x1x2(40 x1 + 20 x2)--- Content provided by FirstRanker.com ---
Where H is in J/mol. For the stated temperature and pressure, determine :- Expressions for H1 and H2 in terms of x1.
- Numerical values for the pure component enthalpies H1 and H2.
- Numerical values for the partial molar enthalpies at infinite dilution.
- A mixture of 1 mol CO & 1 mol water vapour is undergoing the water-gas shift reaction at a temperature of 1100 K and a pressure of 1 bar.
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CO (g) + H20 (g) = CO2 (g) + H2 (g)
The equilibrium constant for the reaction is K = 1. Assume that the gas mixture behaves as ideal gas. Calculate :- The fractional dissociation of steam.
- The fractional dissociation of steam if the reactant steam is diluted with 2 mol nitrogen.
NOTE : Disclosure of Identity by writing Mobile No. or Making of passing request on any page of Answer Sheet will lead to UMC against the Student.
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This download link is referred from the post: PTU B.Tech Question Papers 2020 March (All Branches)
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