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Download GTU BE/B.Tech 2018 Winter 3rd Sem New 2133606 Material And Energy Balance Calculations Question Paper

Download GTU (Gujarat Technological University) BE/BTech (Bachelor of Engineering / Bachelor of Technology) 2018 Winter 3rd Sem New 2133606 Material And Energy Balance Calculations Previous Question Paper

This post was last modified on 20 February 2020

GTU BE/B.Tech 2018 Winter Question Papers || Gujarat Technological University


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Seat No.: Enrolment No.

GUJARAT TECHNOLOGICAL UNIVERSITY

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BE - SEMESTER-III (New) EXAMINATION — WINTER 2018

Subject Code: 2133606 Date:12/12/2018

Subject Name: Material & Energy Balance Calculations

Time: 10:30 AM TO 01:00 PM Total Marks: 70

Instructions:

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  1. Attempt all questions.
  2. Make suitable assumptions wherever necessary.
  3. Figures to the right indicate full marks.
Marks
Q.1
(a) Define the quantities with SI units: i) Force ii) Pressure iii) Work. 03
(b) A force of 20 kgf is applied on a piston of diameter 5 cm. Find the pressure exerted on a piston in KPa. 04
(c) A chemist is interested in preparing 500 ml of 1 normal, 1 molar and 1 molal solution of H2SO4. Assuming the density of H2SO4 solution to be 1.075 g/cm³, calculate the quantities of H2SO4 to be taken to prepare these solutions. 07
Q.2
(a) Define the laws with their equations: 1) Ideal Gas Law ii) Raoult’s Law iii) Henry’s Law 03
(b) A certain quantity of a gas contained in a closed vessel of volume 1 m³ at a temperature of 298 K (25°C) and pressure of 131.7 KPa is to be heated such that the pressure should not exceed 303.98 KPa. Calculate the temperature of gas attained. 04
(c) Derive: Pressure%=Mole%=Volume% 07
OR
(c) A weight of 1.10 kg of Carbon dioxide occupies a volume of 0.033 m³ at 300 K. Using the Van der Waals equation of state, calculate the pressure. Data: For CO2 gas, take a = 3,60.[(m³)² .kPa] / (kmol)² and b=4.3 x 10?² m³ /kmol. 07
Q.3
(a) Derive: pmix= (PMave) /RT 03
(b) A gas mixture contains 0.274 kmol of HCl, 0.337 kmol of N2 and 0.089 kmol of O2. Calculate: (a) Average molecular weight of gas. 04
(c) A solution containing 55% benzene, 28% toluene and 17% xylene by weight is in contact with its vapour at 373 K. Calculate the total pressure and molar composition of the liquid & vapour. Data: Vapour Press. Data at 373 K: Benzene: 178.60KPa, Toluene: 74.60KPa, Xylene: 28KPa. 07
OR
Q.3
(a) Define the terms: (a) % Conversion (b) % Yield (c) % Excess 03
(b) In the production of sulphur trioxide, 100 kmol of SO2, 200 kmol O2 are fed to reactor. The product stream is found to contain 80 kmol SO3. Find the % conversion of SO2. SO2 + 1/2 O2 = SO3 04
(c) In the manufacture of acetic acid by oxidation of acetaldehyde, 100 kmol of acetaldehyde is fed to the reactor per hour. The product leaving the reactor contains 14.81% acetaldehyde, 59.26% acetic acid, and the rest oxygen (on mole basis). Find the percentage conversion of acetaldehyde. CH3CHO + 1/2 O2 = CH3COOH 07
Q.4
(a) Define the following terms: 1) Limiting Reactant ii) Excess Reactant iii) Stoichiometric Ratio 03
(b) Calculate the following for the reaction: C2H6 + 2Cl2 ? C2H4Cl2 + H2 + HCl (1) The stoichiometric ratio of Cl2 to C2H6 (ii) If 4 kmol Cl2 is used per kmol of C2H6, find the % excess Cl2. 04
(c) A coke is known to contain 90% carbon and 10% non-combustible ash(by weight): C + O2 = CO2 1) Find the moles of oxygen theoretically required to burn 100 kg of coke completely. ii) If 50% excess air is supplied, find the analysis of the gases at the end of the combustion? 07
OR
Q.4
(a) Define the following terms: i) Law of Conservation of Mass ii) Heat Capacity iii) recycling 03
(b) Explain the following unit operations with their block diagram and material balances: 1) Distillation ii) Evaporation. 04
(c) Fresh juice contains 15% solids and 85% water by weight and is to be concentrated to contain 40% solids by weight. In a single stage evaporation system, it is found that volatile constituents of juice escape with water leaving the concentrated juice with a flat taste. In order to overcome this problem, part of the fresh juice bypasses the evaporator. The operation is shown schematically: 07
 
Calculate: 1) The fraction of juice that bypasses the evaporator. ii) The concentrated juice produced (containing 40% solids) per 100 kg of fresh juice fed to the process.
Q.5
(a) Explain standard heat of reaction and standard heat of combustion. 03
(b) Explain the significance of bypass operation with neat flow diagram. 04
(c) Soyabean seeds are extracted with the hexane in batch extractors. The flaked seeds are found to contain 18.6% oil, 69% solids, 12.4% moisture (by weight). At the end of the extraction process, cake is separated from hexane-oil mixture. The cake is analyzed to contain 0.8% oil, 87.7% solids and 11.5% moisture (by weight). Find the percent recovery of oil. 07
OR
Q.5
(a) Define: i) Dry-bulb temperature ii) Wet-bulb temperature. 03
(b) Chlorinated diphenyl is heated from 313 K (40°C) to 533 K (260°C) in an indirectly fired heater at the rate of 4000 kg/h. Calculate the heat required to be added to the fluid in the heater. The heat capacity of the fluid in this temperature range is given by the equation: C= 0.7511+1.465x10?³ T, kJ/(kg.K) where T is in K. 04
(c) Calculate the change in enthalpy between reactants and products if both are at 298 K (25°C) and if 5 mole of ethylene oxide is produced as per the following reaction: C2H4(g) + 1/2 O2 = C2H4O(g) 07
Data:
Component ?H°f, kJ/mol at 298.15 K(25°C)
C2H4(g) 52.50
C2H4O(g) -52.63

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