Wednesday, December 9, 2015

PROCESS CALCULATIONS,University Of Pune Question Paper,S.E. (Petroleum/Petrochemical/Polymer) (Sem. – II),2011 Question Paper

PROCESS CALCULATIONS,University Of Pune Question Paper,S.E. (Petroleum/Petrochemical/Polymer) (Sem. – II),2011 Question Paper
University Of Pune Question Paper
S.E. (Petroleum/Petrochemical/Polymer) (Sem. – II) Examination, 2011
PROCESS CALCULATIONS
(2003 Course)
Time : 3 Hours Max. Marks : 100
Instructions: 1) Answers 3 questions from each Section.
2) Answers to the two Sections should be written in separate
books.
3) Neat diagrams must be drawn wherever necessary.
4) Figures to the right indicate full marks.
5) Use of logarithmic tables, slide rule, Mollier charts, electronic
pocket calculator and steam tables is allowed.
6) Assume suitable data, if necessary.
SECTION – I
1. a) Small animals such as mice can live at reduced air pressures down to 20 kPa.
In a test mercury manometer attached to a tank inside which a mouse is kept,
reads differential pressure of 64.5 cm. Hg. The barometer reading of the room
is 100 kPa. Will the mouse survive ? 6
b) 164.5 gm of barium chloride (BaCl2) is dissolved in 135 ml of water. Obtain
the salt concentration in wt % and in normality. 6
[Atomic Weight of Ba = 137.34, Cl = 35.45]
c) Define : Molality and Normality. 4
OR
2. a) An binary mixture contains 92% (by weight) of ethanol and rest water. Obtain
the composition in mol percentage. Also evaluate mol fraction of water
present. 6
b) If 6.5 gm of sugar (sucrose) be dissolved in 135 ml of water, what will be
concentration in wt% and in terms of molarity ? 4
c) An aqueous solution of oxalic acid of 32% concentration (by weight) has
density of 1.34 kg/lit at 25°C. Calculate normality, molality and molarity of the
solution. 6
P.T.O.
[3962] – 348 -2-
3. a) A mixed acid containing 65% (by wt) H2SO4, 20% HNO3 and rest water is
to be made by blending following liquids : 10
i) A spent acid containing 10% HNO3, 60% H2SO4 and rest water.
ii) A concentrated nitric acid containing 90% HNO3, rest water.
iii) Concentrated sulfuric acid containing 98% H2SO4 and rest water.
How many kgs of each of the three available acid streams must be used to obtain
1000 kg of mixed acid ?
b) A mixture of gases contains 10.5% CO2, 13.0% Cl2, 12.7% N2 and rest
hydrogen (all in mol %). 6
i) Determine average molecular weight of the gas.
ii) Calculate the gas composition in weight fractions.
OR
4. a) To prepare a solution of 50% sulfuric acid, a dilute waste acid containing 28%
H2
SO4
 is fortified with a purchased acid of 96% H2
SO4
. How many kilograms
of purchased acid must be bought for each 100 kg dilute acid ? 4
b) Acetylene gas is produced according to the following reaction : 6
CaC2 + 2 H2O → C2H2 + Ca(OH)2.
Calculate number of hours of service that can be derived from 1 kg of calcium
carbide in an acetylene lamp burning 0.1 m3 of gas per hour at temperature of
298 K and pressure of 99.32 kPa.
c) Define : Limiting Reactant, Yield and Selectivity. 6
5. a) Define : Saturation Pressure, Relative Humidity, Humid Volume. 6
b) An air-tight room having volume of 17.86 m3 at 1 atm pressure. Calculate
partial volume of components in the room and partial pressures of individual
components. 6
c) Define Bubble Point and provide stepwise procedure of obtaining Bubble
Point for a multi-component mixture. 6
OR
6. a) The solubility of barium nitrate at 100 °C is 34g/100 g of water. And at 0 °C is
5.0g/100 g of water. If you start with 100 g of Ba (NO3
)
2
 and make a saturated
solution in water at 100 °C, how much water is required ? The precipitated
crystals carry along with them on their surface 4 g of water per 100 g of
crystals. 10
[Atomic Weight of Ba = 137.34].
b) 100 kg of mixture F containing 50% Ethanol, 40% water and rest Methanol
(all in wt. %) flashed to produce P kg of 80% Ethanol, 5% water and rest
Methanol and W kg of 5% Ethanol, 92.5% water and 2% Methanol. Evaluate
P and W. 8
SECTION – II
7. a) Discuss Proximate and Ultimate analysis of coal. 6
b) Propane is mixed with oxygen to obtain a gas containing 67.80% C3H8 and
rest O2 that is burned in an engine with 200% excess air. 82% of the propane
produces CO2, 12.5% goes to CO and rest remains unburned. Calculate
composition of the exhaust gas on a wet basis. 10
OR
8. a) If 300 kg of air and 24 kg of carbon are fed to a reactor at 460°C and after
complete combustion no material remains in the reactor, how many kgs of
carbon will have been removed ? How many kgs of oxygen ? How many kgs
total ? 8
b) Aviation gasoline is iso-octane C8H18. If it is burned with 20% excess air and
30% of the carbon forms carbon monoxide, what is Orsat analysis ? 8
9. a) A synthesis gas analyzing 6.4% CO2
, 0.2% O2, 40% CO and 50.8 % H2
 and
rest N2
 is burned with 40% dry excess air. What is the composition of the
flue gas ? 8
b) The molar heat capacity of Cumene is given by 10
Cp = 139.2 + 53.76×10–2 T – 39.79×10–5 T2 where Cp is in kJ/(kmol.K) and
T is in K.
i) Calculate the mean molar heat capacity in the temperature range of
300 – 1000 K.
ii) Cumene enters a heat exchanger at a rate of 450 m3/hr at STP. Calculate
the heat to be supplied to the gas to raise its temperature from 400 to 700 K.
OR
10. a) What is adiabatic flame temperature ? How it is determined ? Discuss its
importance. 6
b) Discuss following :Combustion, Orsat, Analysis. 6
c) A stream flowing at rate of 132.5 mol/hr containing 72.5 mole % N2 and rest
H2 is to be heated from 25°C to 230°C . Calculate total quantity of heat to be
transferred. Cp data are as follows : 6
Gas a b×103
c×106
N
2
25.591 −5.41 13.183
H
2
28.61 1.02 − 0.15
11. a) An irn pyrite ore containing 85% FeS2
 and 15% gaunge (inert, dirt, rock etc.)
is roasted with an amount of air equals to 200% excess air according to the
reaction
4FeS2 + 11 O2 → 2 Fe2O3 + 8 SO2
In order to produce SO2. All the gauge plus Fe2O3 end up in the solid waste
product (cinder), which on analysis shows 4% FeS2. Determine the standard
heat of reaction per kilogram of ore. 8
b) A tank contains 10 m3
 of fresh water. Brine having a concentration of 10 kg
salt/m3 is sent into the tank at the rate of 250 lit/min. The mixture is kept
uniform by mixing and runs out at a rate of 120 lit/min. Calculate the exit
brine concentration when tank contains 20 m3
 of brine. 8
OR
12. a) Hydrochloric acid is an important industrial chemical. To make aqueous
solution of it of commercial grade (called muriatic acid), purified HCl (g) is
absorbed in water in a tantlum absorber in a continuous process. How much
heat is to be removed from the absorber per 100 kg of product if hot HCl (g)
at 120°C is fed into water in the absorber. The feed water can be assumed to
be at 25 °C and the exit product HCl (aq.) is 25% HCl (by wt) at 35°C
Data: Cp for HCl (g) = 29.13 – 0.1341×10–2 T + 0.9715×10–2 T2
where, Cp is in kJ/ (kmol. K) with T in K
Cp for product is approximately 2.7 kJ/ (kg. K) 8
b) A square tank 4 m on a side and 10 m high is filled to the brim with water.
Find the time required for it to empty through a hole in the bottom 5 cm2 in
area. 8
——————

S.E. (Chemical) (Semester – I),University Of Pune Question Paper,2011 Question Paper,PROCESS CALCULATIONS

S.E. (Chemical) (Semester – I),University Of Pune Question Paper,2011 Question Paper,PROCESS CALCULATIONS
University Of Pune Question Paper
S.E. (Chemical) (Semester – I) Examination, 2011
PROCESS CALCULATIONS
(2003 Course) (Common to Biotech)
Time : 3 Hours Max. Marks : 100
 Instructions : I) Answers to the two Sections should be written in
separate books.
II) Neat diagrams must be drawn wherever necessary.
III) Black figures to the right indicate full marks.
IV) Use of logarithmic tables, slide rule, Mollier charts,
electronic pocket calculator and steam tables is
allowed.
V) Assume suitable data, if necessary.
SECTION – I
1. a) The iron metal whose weight is 500 pounds occupies a volume 29.25 litres,
calculate the density of iron metal expressed in kg / m3. 4
b) Determine the weight percentage of the constituent elements of potassium
sulphate. 4
c) Carburetted water gas has the following composition by volume : Hydrogen
35.2 %, Methane 14.8 %, Ethylene 12.8 %, Carbon dioxide 1.5 %, Carbon
monoxide 33.9 % and Nitrogen 1.8 %. The gas is available at 101.3 kN / m2
and 300 K. Express the composition by wt % and determine the average
molecular weight and density of the gas. 8
OR
2. a) A compound is found to contain 62.4 % Ca and 37.6 % C.
i) How many gram atoms of Ca and C present in 100 gm of the compound ?
ii) Suggest an empirical formula for the compound. 6
b) Calculate the molality of a solution of 93 % H2SO4 (W/V). The density of
the solution is 1840 kg / m3. 5
c) A sample of limestone is found to contain 54.5 % CaO (by mass). If this
CaO is present as CaCO3 in the limestone, find the content of CaCO3 in the
limestone. 5
3. The feed to an absorption column consists of 20 % H2S and the balance inert.
Only H2S is removed from the gas by absorbing in an alkaline solution. The gas
enters the absorber at 600 kPa and 310 K and leaves at 500 kPa and 290 K
containing 2 % H2S. If H2S is removed at the rate of 100 kg / hr, calculate
i) the volume of gas (in m3) entering per hour, ii) the volume of gas (in m3)
leaving per hour, iii) percentage recovery of H2S. 16
OR
4. a) Crystals of MgCl2.6H2O have solubility of 190 gm per 100 gm ethanol at
298.15 K. It is desired to make 1000 kg of saturated solution. Calculate the
quantities of the crystals and ethanol required to make the above solution.
Also, find the composition of saturated solution by mass. 8
b) A mixture of CuSO4.5H2O and FeSO4.7H2O weighs 100 gm. It is heated in
an oven at 378 K to evaporate water of hydration. The mass of mixture after
removal of water is 59.78 gm. Calculate the mass ratio of CuSO4 to FeSO4
in the mixture. 8
5. Pure sulphur is burnt in a burner at the rate of 0.3 kg/sec. Fresh dry air is
supplied at 303 K and 100 kPa. The gases from the burner contain 16.5 % SO2,
3.5 % O2 and rest N2 on SO3 - free volume basis. The gases leave the burner at
1073 K and 101.3 kPa absolute. Calculate (a) the fraction of sulphur burnt into
SO3 (b) the percentage excess air over the amount required to oxidise the sulphur
to SO2 and (c) the volume of dry air in m3/sec. 18
OR
6. A mixture of pure carbon dioxide and hydrogen is passed over a nickel catalyst.
The temperature of the catalyst bed is 588 K and the reactor pressure is 2 MPa g.
The analysis of the gases leaving the reactor showed CO 57.1 %, H2 41.1 %,
CH4 1.68 % and CO 0.12 % (by volume) on a dry basis. The reactions taking
place in the reactor are :
 CO2 + 4 H2 = CH4 + 2 H2O
and CO2 + H2 = CO + H2O
Find (a) the conversion of CO2 per pass (b) yield of CH4 in terms of CO2
reacted and (c) the composition of the feed. 18
SECTION – II
7. a) Heat capacity of gaseous SO2 is given by
0 Cmp = 43.458 + 10.634 × 10−3 T − 5.945 × 105 T −2 kJ / kmol.K
Calculate the heat required to raise the temperature of 1.0 kg pure SO2 from
300 to 1000 K. 8
b) In the ferrite process for the manufacture of caustic soda, soda ash and
gangue from pyrites roaster are mixed and heated. The following reaction
takes place and CO2 evolves. Calculate the standard heat of reaction at 298.15 K.
Na2CO3 (s) + Fe2O3 (s) = Na2O.Fe2O3 (s) + CO2 (g)
Given Data : Std Heat of formation at 298.15 K
Component H kJ / mol Δ f
1. Na2CO3 (s) − 1130.68
2. Fe2O3 (s) − 817.30
3. Na2O.Fe2O3 (s) − 1412.20
4. CO2 (g) − 393.51 8
OR
8. Oil is to be extracted from meal by a continuous counter-current extractor. The
unit is charged with 1000 kg/hr meal based on oil-free solids. Untreated meal
contains 0.4 kg oil and 0.025 kg benzene per kg oil-free meal. A fresh solvent is
benzene containing 1.5 % oil (mass %). The ratio of the fresh solvent to the oilfree
meal is kept at 0.065 kg/kg. The solid meal retains 0.507 kg solution per kg
solid. The solution retained by the meal contains 11.83 % oil (by mass). Make a
complete material balance and find the composition and the amount of overflow
from the extractor. 16
9. An air conditioning plant is employed to maintain 300 K DBT and 50 % RH in
an auditorium. The air flow rate to the auditorium is measured to be 5.806 m3 / sec
at 290 K at 83.5 % RH. The effluent air from auditorium is partially recycled and
is mixed with the incoming fresh air. The fresh air is fed at the rate of 1.25 m3 / sec
at 308 K having 70 % RH. The mixed air is found to have 302.5 K at DBT and
54 % RH and is passed through a/c plant to make it suitable for auditorium. The
total pressure can be assumed to be 101.3kPa.
Calculate :
a) Moisture added in auditorium / removed in a/c plant.
b) The recycle ratio.
c) Moles of air recycled per mole of fresh ambient air. 18
OR
10. a) A solution of ethyl alcohol containing 8.6 % alcohol is fed at the rate of
1000 kg / h to a continuous distillation column. The product (distillate) is a
solution containing 95.5 % alcohol. The waste solution from the column carries
0.1 % of alcohol. All percentages are by mass. Calculate the mass flow rates
of top
and bottom products in kg / h and the percentage loss of alcohol. 10
b) A crystallizer is charged with 7500 kg of an aqueous solution at 377 K, 29.6 %
by mass of which is anhydrous sodium sulphate. The solution is cooled.
During the cooling operation 5 % of the initial water is lost by evaporation.
As a result, crystals of Na2SO4.10 H2O crystallize out. If the mother liquor
is found to contain 18.3 % (by mass) anhydrous Na2SO4. Calculate the yield
of crystals and the quantity of mother liquor. 8
11. A coal sample from Godavari colliery has the following proximate and ultimate
analyses.
Proximate Analysis mass % Ultimate Analysis mass %
Moisture 7.0 Carbon 54.0
Volatile matter 26.0 Hydrogen 3.0
Fixed Carbon 46.0 Sulphur 0.4
Ash 21.0 Nitrogen 2.2
Ash 21.0
Oxygen (by diff) 19.4
The gross calorific value = 23392 kJ / kg at 298.15 K.
Calculate :
a) The net hydrogen in the coal,
b) The combined water in the coal,
c) GCV based on the Dulong formula, and
d) NCV of the coal. 16
OR
12. The purge gas obtained from ammonia synthesis loop has the composition
H2 – 69 %, N2 – 23 %, Ar – 2.7 %, and CH4 – 5.3 % (mole basis). It is burnt
with 20 % excess air. Calculate (a) the GCV and NCV at 298.15 K of the purge
gas, (b) theoretical air required, and (c) the molar composition of the flue gases.
GCV and NCV of CH4 is 890.65 and 802.62 kJ / mol respectively.
Latent heat of water vapour at 298.15 K = 2442.5 kJ / kg. 16
Atomic weights : Fe = 55.8, Ca = 40, Na = 23, K = 39, S = 32, Mg = 24, Cu = 63.5.
————————

Search Everything Here