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IC engine and RAC Test 1

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IC engine and RAC Test 1
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  • Question 1
    2 / -0.33
    An ideal petrol engine produce 0.98 kJ of work after consuming 0.070 gm of fuel. The calorific value of fuel is 43757 kJ/kg. What is the required compression ratio if specific heat air is assumed constant?
    Solution

    Concept:

    Heat supplied = mass of fuel burnt × Calorific value

    Qs = ṁ × C.V

    Qs = 0.070 × 10-3 × 43754

    Qs = 3.06299 kJ

    Now,

    \({\rm{Thermal\;efficiency\;}} = \frac{{{W_{net}}}}{{{Q_{supplied}}}} = 1 - \frac{1}{{{r^{\gamma - 1}}}}\)

    Calculation:

    \({\eta _T} = \frac{{0.98}}{{3.06299}}\)

    \(\therefore {\eta _T} = 1 - \frac{1}{{{r^{0.4}}}}\)

    r = 2.622

  • Question 2
    2 / -0.33

    A sample of air at 35°C and standard atmospheric pressure is taken. Then sample has 70% relative humidity

    If the saturation pressure is 5.628 kPa, then the amount of moisture in kg/kg of dry air is
    Solution

    Concept:

    Relative humidity, ϕ = 0.70, Saturation pressure, Ps = 5.628 kPa

    Standard atm. Pressure P = 101.325 kPa

    ϕ = Pv/Ps (Calculate Pv)

    \({\rm{Specific\;humidity\;}}\left( \omega \right) = \frac{{0.622\;{P_v}}}{{P - {P_v}}}\)

    Calculation:

    \(\phi = 0.70 = \frac{{{P_v}}}{{5.628}}\) 

    Pv = 3.9396 kPa

    \(\omega = \frac{{0.622\; \times \;3.9396}}{{101.325\; - \;3.9396}}\)

    ∴ ω = 0.025 kg/kg of d.a. 
  • Question 3
    2 / -0.33
    If room sensible heat = 10 kW and latent heat = 70 kW, then room sensible heat factor is
    Solution

    Concept:

    The sensible heat factor is the ratio of Sensible heat to the Room total heat.

    Room total heat = Sensible heat (SH) + Latent heat (LH)

    Sensible Heat Factor is given by, 

    \(SHF = \frac{{SH}}{{LH + SH}} \)

    Calculation:

    Given, SH = 10 kW, LH = 70 kW

    \( SHF = \frac{{10}}{{70 + 10}} = \frac{{10}}{{80}} = 0.125\)

  • Question 4
    2 / -0.33
    The chemical formula for refrigerant R – 114 is
    Solution

    Concept:

    Formula for naming of refrigerant,

    R (m - 1) (n + 1)P,

    When, m → number of carbon atoms

    n → Number of hydrogen atoms

    P → Number of fluorine atoms

    Here,

    m – 1 = 1 → m = 2

    n + 1 = 1 → n = 2

    P = 4

    So, there are 2 C, zero H, 4F and remaining balance by Cl.

    Therefore, chemical formula is C2 Cl2 F4
  • Question 5
    2 / -0.33
    The compressor work in a refrigerating machine with throttle valve is 20 kJ/kg, by using expander the increase in net refrigerating effect is 3.5 kJ/kg. The percentage change in work is____
    Solution

    Concept:

    Compressor work with expansion valve = 20 kJ/kg

    When expander is placed in place of expansion valve.

    ∴ Net compression work = 20 – 3.5

    ∴ Net compression work = 16.5 kJ/kg

    Now,

    \({\rm{\% \;change\;in\;work\;}} = \frac{{16.5 - 20}}{{20}} \times 100\)

    ∴ Change in work = -17.5%

  • Question 6
    2 / -0.33
    The compression ratio of air standard Otto cycle is 8. The initial conditions of air at the beginning of the compression stroke are 300K and 0.2MPa. The amount of energy added during the combustion process is 25kJ/mol.  Work done(kJ) per mole of air ____
    Solution

    Concept:

    \(\eta = \frac{{Work\;done}}{{Heat\;input}}\)

    \(\eta = 1 - {\left( {\frac{1}{r}} \right)^{\gamma - 1}}\) 

    Calculation:

    \(\eta = 1 - {\left( {\frac{1}{r}} \right)^{\gamma - 1}}\) 

    \(\eta = 1 - {\left( {\frac{1}{8}} \right)^{0.4}}\) 

    ∴ η = 56.47%

    Now,

    Work done = η × Q1

    Work done = 0.5647 × 25

    ∴ Work done = 14.12 kJ/mol

  • Question 7
    2 / -0.33
    The supply air temperature is 15˚C and apparatus dew point is 12˚C for the cooling coil with bypass factor of 0.15. What is temperature (˚C) at inlet of cooling coil?
    Solution

    Concept:

    \({\rm{Bypass\;factor\;}} = \frac{{{T_s} - DPT}}{{{T_i} - DPT}}\)

    Ts = temperature of supply air, Ti = temperature at inlet of cooling coil, DPT = Dew point temperature

    Calculation:

    \(0.15 = \frac{{15 - 12}}{{{T_i} - 12}}\)

    ∴ Ti – 12 = 20

    ∴ Ti = 32°C 
  • Question 8
    2 / -0.33

    Moist air with DBT = 40°C and relative humidity of 60 % is compressed to 5.05 bar and DBT = 150° C.

    Using the following data, find the relative humidity of compressed air ______%.

    RH2O = 462 J/kg k, Ps at 40° C = 7.384 kPa, Ps at 150° C = 4.76 bar, Atm. Pressure = 1.01 bar (round off to two decimals)

    Solution

    Concept:

    Relative humidity, ϕ = Pv/Ps

    \({\rm{Specific\;humidity\;}}\left( \omega \right) = \frac{{0.622\;{P_v}}}{{P - {P_v}}}\)

    Calculation:

    Patm = 101 kPa

    Ts = 40°C Ps = 7.384 kPa

    ϕ1 = 0.6 = Pv/Ps

    Pv1 = 4.430 kPa

    \(\omega = \frac{{0.622\; \times \;4.4304}}{{101 - 4.4304}}\)

    ω = 0.0285 kg vap./kg of dry air

    In compression, ω remains constant

    ω1 = ω2

    \(0.0285 = \frac{{0.622\;{P_{v2}}}}{{P - {P_{v2}}}}\)

    \(\frac{{0.622\;{P_{v2}}}}{{505 - {P_{v2}}}} = 0.0285\)

    Pv2 = 22.1252 kPa

    ϕ2 = 22.1252/476

    ϕ2 = 0.04648 ~ 4.65%

  • Question 9
    2 / -0.33
    Dry bulb temperature of the air is 25°C and dew point temperature at 1 atm pressure is 20°C. The saturation pressure of water at 20°C and 25°C are 0.02462 bar and 0.03813 bar respectively. The specific heat of the air and water vapour are 1.005 and 1.88 kJ/kgK respectively and latent heat of vaporization of water at 0°C is 2500 kJ/kg. The enthalpy (in J/kg) of air is
    Solution

    Concept:

    h = 1.005 t + ω (2500 + 1.88t)

    Calculation:

    Given:

    P = 1 atm = 1.013 bar and Pv = 0.02462 (at DPT)

    Now,

    specific humidity \((\omega) = \frac{{0.622{P_v}}}{{P - {P_v}}} \) 

    \(\omega = \frac{{0.622 \times 0.02462}}{{1.013 - 0.02462}}\)

    ∴ ω = 0.01549 kg/kg of dry air

    Now,

    Enthalpy (h) = 1.005 t + ω (2500 + 1.88t)

    h = 1.005 × 25 + 0.01549 (2500 + 1.88 × 25)

    ∴ h = 64.42 J/kg of dry air.
  • Question 10
    2 / -0.33
    An engine based on a standard Otto cycle is operating with air as an medium with specific heat of 1.4 has a cylinder diameter of 5 cm and stroke length of 7.5 cm. If the clearance volume is 88.15 cc and the heat supplied per kg of air per cycle is 900 kJ/kg, then work output (in kJ) per kg of air is?
    Solution

    Concept:

    In a otto cycle efficiency is given as

    \(η = 1 - {\left( {\frac{1}{r}} \right)^{\gamma - 1}}\)

    Where r is the compression ratio and γ is the ratio of specific heat

    Also compression ratio

    \(r = \frac{{volume\;before\;compression}}{{volume\;after\;compression}} = \frac{{{V_s} + {V_c}}}{{{V_c}}}\)

    Vs = Stroke volume or volume of cylinder = \(\frac{\pi }{4}\;{d^2}\;l\)

    Vc = Clearance volume

    Where d is the diameter of the cylinder and l is the stroke length

    Also

    \(η = \frac{{Work\;ouput}}{{Heat\;Supplied}}\)

    Calculation:

    Given:

    γ = 1.4, Vc = 88.15 cc, d = 5 cm, l = 7.5 cm

    Heat Supplied = 900 kJ/kg

    \({V_s} = \frac{\pi }{4}\;{d^2}\;l = \frac{\pi }{4} \times {5^2} \times 7.5 = 147.262\;cc\)

    \(r = \frac{{{V_s} + {V_c}}}{{{V_c}}} = \frac{{88.15 + 147.262}}{{88.15}} = 2.674\)

    ∴ r = 2.674

    Now

    \(η = 1 - {\left( {\frac{1}{{2.674}}} \right)^{1.4 - 1}} \)

    ∴ η = 0.325

    Now,

    Work Output = η × Heat input

    Work Output = 0.325 × 900

    ∴ Work Output = 292.5 kJ/kg

  • Question 11
    2 / -0.33
    A car has 4 cylinder engine of 80 mm bore and 90 mm stroke, what is the clearance volume of each cylinder and the cubic capacity of engine if compression ratio is 8?
    Solution

    Concept:

    \({\rm{Cubic\;capacity\;of\;engine\;}} = \frac{\pi }{4}{d^2}L \times {\rm{No}}.{\rm{\;of\;cylinders}}\)

    Where

    \({V_s} = \frac{\pi }{4}{d^2}L = {\rm{\;displacement\;volume\;or\;swept\;volume}}\)

    \({\rm{Compression\;ratio\;}}\left( r \right) = \frac{{{V_c} + {V_s}}}{{{V_c}}}\)

    Vc = clearance vol.

    Calculation:

    \({V_s} = \frac{\pi }{4}{d^2}L\)

    \({V_s} = \frac{\pi }{4}\left( {{{0.08}^2}} \right)\left( {0.09} \right)\)

    Vs = 4.5238 × 10-4 m3

    Vs = 0.45238 × 10-3 × 106 cm3

    Vs = 452.38 cc

    Now,

    Total cubic capacity = 4 × 452.38

    Total cubic capacity = 1809.56 cc

    Now,

    \(r = 8 = \frac{{{V_c} + {V_s}}}{{{V_c}}} \Rightarrow {V_L} = \frac{{{V_s}}}{{r - 1}}\)

    VL = 64.63 cc

  • Question 12
    2 / -0.33

    44 kg of C3H8 is burnt with 1160 kg of air (Mol. Wt. = 29) to produce 88 kg of CO2 and 14 kg of CO

    \({C_3}{H_8} + 5{O_2} = 3C{O_2} + 4{H_2}O\) 

    What is the percent excess air used?

    Solution

    Calculation:

    \({\rm{Actual\;air}} - {\rm{fuel\;ratio\;}} = \frac{{Actual\;air\;\left( {kg} \right)}}{{fuel\;\left( {kg} \right)}}\)

    \({\left( {AF} \right)_{actual}} = \frac{{1160}}{{44}} = 26.36\)

    Now,

    \({\rm{Stoichiometric\;air\;fuel\;ratio}} = \frac{{5\left[ {{O_2} + 3.76\;{N_2}} \right]}}{{{C_3}{H_8}}}\)

    \({\rm{Stoichiometric\;air\;fuel\;ratio}} = \frac{{5\left[ {2 \times 16 + 3.76 \times 28} \right]}}{{3 \times 12 + 1 \times 8}}\)

    ∴ Stoichiometric air fuel ratio = 15.6

    Now,

    \(Percentage\;excess\;air = \frac{{Actual\;AF\;ratio}}{{stociometric\;AF\;ratio}} \times 100 - 100\)

    \(Percentage\;excess\;air = \left( {\frac{{26.36 - 15.6}}{{15.6}}} \right) \times 100\)

    ∴ Percentage excess air = 68.9 %

  • Question 13
    2 / -0.33

    Air enters a duct at 15°C and 80% relative humidity and leaves at 30°C with a flow rate of 2.5 m3/s. If the air remains constant at 101.3 kPa, then the rate of heat transfer is

    (Psat at 15°C = 1.6 kPa and at 30°C = 4.3 kPa)
    Solution

    Concept:

    Enthalpy of moist air,

    h = 1.005 td + ω(2500 + 1.88 td) (td → dry bulb temperature in °C)

    Heat transfer rate, Q = ṁa (h2 – h1)

    Calculation:

    Given:

    T1 = 15°C = 288 K, T2 = 30°C = 303 K, ϕ1 = 0.8, V̇ = 2.5 m3/s, Pt = 101.3 kPa,

    \({P_{{s_1}}} = 1.6\;kPa,\;{P_{{s_2}}} = 4.3\;kPa\) 

    Now,

    \({\phi _1} = 0.8 = \frac{{{P_{{v_1}}}}}{{{P_{{s_1}}}}}\)

    \(0.8 = \frac{{{P_{{v_1}}}}}{{1.6}}\)

    \(\therefore {P_{{v_1}}} = 1.28\;kPa\) 

    Now,

    \({\rm{Specific\;humidity\;}}\left( {{\omega _1}} \right) = \frac{{0.622\;\;{P_{{v_1}}}}}{{{P_t} - {P_{{v_1}}}}}\)

    \({\omega _1} = \frac{{0.622 \times 1.28}}{{101.3 - 1.28}}\)

    ω1 = 7.96 × 10-3 kg/kg of dry air

    As no moisture is added or removed,

    ω1 = ω2 = 7.96 × 10-3

    Now,

    Enthalpy of moist air of entry,

    h1 = (1.005 × 15) + 7.96 × 10-3 × (2500 + 1.88 × 15)

    h1 = 35.199 kJ/kg

    h2 = (1.005 × 30) + 7.96 × 10-3 × (2500 + 1.88 × 30)

    h2 = 50.498 kJ/kg

    Now,

    Mass flow rate of dry air,

    \({\dot m_a} = \frac{{{P_a}\dot V}}{{{R_a} \cdot {T_1}}} = \frac{{\left( {101.3 - 1.28} \right)5}}{{0.287 \times 288}}\)

    a = 3.025 kg/s

    Now,

    Heat transfer rate = ṁa (h2 – h1)

    Heat transfer rate = 3.025 × (50.498 – 35.199)

    Heat transfer rate = 46.279 kJ/s

    ∴ Heat transfer rate = 46.28 kW
  • Question 14
    2 / -0.33

    More test was conducted for a 2-stroke spark ignition engine having 2 – cylinders and following data is obtained. Brake power = 14 kW Brake Power of individual cylinder = 5.4 kW, 4.80 kW.

    What is the mechanical efficiency of this engine?

    Solution

    Concept:

    Let the cylinders be 1 and 2

    Net brake power bp1,2

    Indicated power = Brake power + Frictional power

    Ip = bp + fp

    \({\rm{Mechanical\;efficiency}} = \frac{{b{p_{1,2}}}}{{i{p_{1,2}}}}\)

    ip1,2 = net indicated power = ip1 + ip2

    Calculation:

    Given:

    bp1,2 = 14 kW, bp1 = 5.4 kW, bp2 = 4.80 kW

    ip1-2 = bp1-2 + fp

    ip1 = bp1 + fp

    ip2 = ip1-2 – ip1

    ip= bp1-2 + fp – bp1 – fp

    ip2 = bp1-2 – bp1

    ip2 = 14 – 5.4

    ip2 = 8.6 kW

    Now,

    ip1 = bp1-2 – bp2

    ip= 14 – 4.8

    ip= 9.2 kW

    Now,

    ip1-2 = 9 – 2 + 8.6

    ip1-2 = 17.8 kW

    Now,

    ηm = bp1-2/ip1-2 = 14/17.8

    ηm = 78.65 % 

  • Question 15
    2 / -0.33
    Heat rejection factor for an ideal refrigerator working on vapor compression refrigeration cycle is 1.55. The heat absorbed in evaporator is found to be 50 kW. Keeping the heat rejection from the condenser as constant, the COP is now increased by 20 %. What will be the work done required (kW) now?
    Solution

    Concept:

    \({\rm{Heat\;rejection\;factor}} = \frac{{Heat\;rejected\;from\;condensor\;\left( {const} \right)}}{{Heat\;absorbed\;by\;evaporator}}\)

    Work = Qcondensor - Qevaporator

    \({\rm{COP}} = \frac{{{Q_{absorbed}}}}{{work\;done}}\;\;\;\;\left( {{\rm{This\;is\;increased\;by\;}}20{\rm{\% }}} \right)\)

    Calculation:

    \(1.55 = \frac{{{Q_{condensor}}}}{{50}}\)

    Qc = 77.5 kW

    W = 77.5 – 50

    W = 27.5 kW

    Now,

    \(COP = \frac{{50}}{{27.5}} = 1.8181\)

    (COP)new = 1.2 × 1.8181

    \(1.2 \times 1.8181 = \frac{{{Q_{condensor}} - W'}}{{W'}}\)

    (2.1818 W’ + W’) = Qc

    \(W' = \frac{{{Q_c}}}{{3.1818}}\)

    W' = 24.357 kW

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