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609 kJ/kg
Ethane
Two kilograms of gas is confined in a m3 tank at 200 kPa and 88°C. What type of gas is in the tank?
333.42 kJ/kg
Find the enthalpy of Helium if its internal energy is 200 kJ/kg.
9.47 kg
Compute the mass of a 2 m3 propane at 280 kPa and 40°C.
200 ft3/min
0.414 m2
110.71 kg/hr
0.286 ft
30%
0.00714 miles
2.55 m
3543.75 kg/hr
2.258 lbs
106.33 × 106 dynes
1793.96 kPag
1 furlong
9.46 kg
1.24 lbs
1647.29 kJ/kg
471 BTU/lb
85%
49.15 TR
14.42
37.50 kW
3.69
40 kW
115.55°C
416.33 K
18.38
11.11%
3365.50°C
215.44 kPa
123.11 kPa
365.88 kPa
111.44 kW
0
0
97.41 kPa
1289.00 m
90.74 kPa
0.0122 moles
314.2 K
97°F
667 kJ
-6232.09 BTU
78.57%
34.59 liters
37,500 lb/hr
1582 kJ/kg
62.11%
-1265.02 kJ/kg
Steam at 2 MPa and 250°C in a rigid cylinder is cooled until the quality is 30%. Find the heat rejected from the cylinder.
@ 2 Mpa and 250°C:
υ = 0.11144 m3/kg
u = 2679.6 kJ/kg
@ 2 Mpa, (saturated):
uf = 0.0011767 m3/kg
uf = 906.44 kJ/kg
ug = 0.09963 m3/kg
ug = 1693.8 kJ/kg
1162.40 kJ/kg
At 1.3 MPa, a mixture of steam and water has an entropy of 3 kJ/kg-K, Find the enthalpy of the mixture.
@ 1.3 MPa:
sf = 2.2515 kJ/kg-K
hf = 814.93 kJ/kg
sg = 6.4952 kJ/kg-K
hfg = 1972.7 kJ/kg
745.92 kJ
A mixture with 70% quality at 500 kPa is heated isothermally until its pressure is 300 kPa. Find the heat added during the process.
@ 600 kPa: sf = 1.8607 kJ/kg-K sfg = 4.9606 kJ/kg-K
@ 300 kPa and 151.86°C: s = 7.0888 kJ/kg-K
785.92 kJ/kg
A tank contains exactly one kilogram of water consisting of liquid and vapor in equilibrium at 1 MPa. If the liquid contains one-third and the remaining is vapor of the volume of the tank, what is the enthalpy of the contents of the tank?
@ 1MPa:
υf = 0.0011273 m3/kg υfg = 0.19444 m3/kg
hf = 762.81 kJ/kg hfg = 2015.3 kJ/kg
2.51 m/s
Water substance at 70 bar and 65°C enters a boiler tube of constant inside diameter of 25 mm. The water leaves the boiler tube at 50 bar and 700 K at velocity of 150 m/s. Calculate the inlet velocity (m/s).
From steam tables:
@ 70 bar (7Mpa) and 65°C: υ1 = 0.001017 m3/kg
@ 50 bar (5Mpa) and 700 K (427°C): υ2 = 0.06081 m3/kg
1.609 L/s
Water substance at 70 bar and 65°C enters a boiler tube of constant inside diameter of 35 mm. The water leaves the boiler tube at 50 bar and 700 K at velocity of 150 m/s. Calculate the inlet volume flow (liters/s).
From steam tables:
@ 70 bar (7Mpa) and 65°C: υ1 = 0.001017 m3/kg
@ 50 bar (5Mpa) and 700 K (427°C): υ2 = 0.06081 m3/kg
3.08%
Steam leaves an industrial boiler at 827.4 kPa and 171.6°C. A portion of the steam is passed through a throttling calorimeter and is exhausted to the atmosphere when the calorimeter pressure is 101.4 kPa. How much moisture is leaving the boiler container if the temperature of the steam at the calorimeter is 115.6°C?
@ 827.4 kPa and 171.6°C: hf = 727.25 kJ/kg hfg = 2043.2 kJ/kg
@ 101.4 kPa and 115.6°C: h2 = 2707.6 kJ/kg
6.2 kJ/kg-K
A throttling calorimeter is connected to a desuperheated steam line supplying steam to the auxiliary feed pump on a ship. The line pressure measures 2.5 MPa. The calorimeter pressure is 110 kPa at 150°C. Determine the entropy of the steam line.
@ 110 kPa and 150°C: h2 = 2775.6 kJ/kg
@ 2.5 MPa: hf = 962.11 kJ/kg hfg = 1841 kJ/kg
sf = 2.5547 kJ/kg-K sfg = 3.7028 kJ/kg-K
449.42°F
3.5%
A certain coal has the following ultimate analysis:
C = 69% N2 = 5% H = 2.5% S =7%
Determine the amount of oxygen if the heating value of fuel is 26,961.45 kJ/kg.
P27,127.76
A diesel engine consumed 945 liters of fuel per day at 35°C. If the fuel was purchased at 15.6°C and 30°API at P29.00/li. Determine the cost of fuel to operate the engine per day.
17.53 days
28.00%
A logging firm in Isabella operates a Diesel Electric Plant to supply its electric energy requirements. During a 2 hour period, the plant consumed 250 gallons of fuel at 80°F and produced 2900 kW-hrs. Industrial fuel is used at 30°API and was purchased at P30/li at 60°F. Determine the overall thermal efficiency of the plant.
1.055
The dry exhaust gas from the oil engine has the following gravimetric analysis:
CO2 = 21.6% O2 = 4.2% N = 74.2%
Specific heats at constant pressure for each component of the exhaust gas in kCal/kg-°C are:
CO2 = 0.203 O2 = 0.219 N = 0.248
Calculate the specific gravity if the molecular weight of air is 28.97 kg/kg-mol.
7.526 lb/lbcoal
A bituminous coal has the following composition:
C = 71.5% H = 5.0% O = 7.0% N = 1.3% S = 3% Ash = 7.6%
W = 3.4%
Determine the theoretical weight of Nitrogen in lb/lb of coal.
1.233 molair/molfuel
A gaseous fuel mixture has a molal analysis:
H2 = 14% CH4 = 3% CO = 27% O2 = 0.6% CO2 = 4.5% N2 = 50.9%
Determine the air-fuel ratio for complete combustion on molal basis.
17.55%
A volumetric analysis of a gas mixture is a follows:
CO2: 12% O2: 4% N2: 80% CO: 4%
What percentage of CO2 on a mass basis?
234,019 m3/hr
The following coal has the following ultimate analysis by weight:
C = 70.5% H2 = 4.5% O2 = 6.0% N2 = 1.0% S = 3.0% Ash = 11%
Moisture = 4%
A stocker fired boiler of 195,000 kg/hr steaming capacity uses this coal as fuel. Calculate volume of air in m3/hr with air at 60°F and 14.7 air pressure if the boiler efficiency is 70% and FE = 1.10.
80.67%
23.5 kg of steam per second at 5 MPa and 400°C is produced by a steam generator. The feedwater enters the economizer at 145°C and leaves at 205°C. The steam leaves the boiler drum with a quality of 98%. The unit consumes 3 kg of coal per second as received having value of 25,102 kJ/kg. What would be the overall efficiency of the unit in percent?
Steam properties:
@ 5 MPa and 400°C: h = 3195.7 kJ/kg
@ 5 MPa: hf = 1154.23 kJ/kg hfg = 1640.1 kJ/kg
@ 205°C: hf = 875.04 kJ/kg
@ At 145°C: hf = 610.63 kJ/kg
25.55%
In a Rankine cycle steam enters the turbine at 2.5 MPa (enthalpies & entropies given) and condenser of 50 kPa (properties given), what is the thermal efficiency of the cycle?
@ 2.5 MPa: hg = 2803.1 kJ/kg sg = 6.2575 kJ/kg-K
@ 50 kPa: sf = 1.0910 kJ/kg-K sfg = 6.5029 kJ/kg-K
hf = 340.49 kJ/kg hfg = 2305.4 kJ/kg
υf = 0.00103 m3/kg
300 kW
25.32 kJ/kg
2.869 kg/s
In an open feedwater heater for a steam plant, saturated steam at 7 bar is mixed with subcooled liquid at 7 bar and 25°C. Just enough steam is supplied to ensure that the mixed steam leaving the heater will be saturated liquid at 7 bar when heater efficiency is 95%.
Steam properties:
@ 7 bar, saturated vapor: hg = 2763.5 kJ/kg
@ 7 bar and 25°C: hf = 105.5 kJ/kg
@ 7 bar, saturated liquid: hf = 697.22 kJ/kg
567 kg/s
79.46%
Steam expands adiabatically in a turbine from 2000 kPa, 400°C to 400 kPa, 250°C. What is the effectiveness of the process in percent assuming an atmospheric pressure of 18°C? Neglect changes in kinetic and potential energy.
Steam properties:
@ 2000 kPa and 400°C: h = 3247.6 kJ/kg s = 7.1271kJ/kg-K
@ 400 kPa and 250°C: h = 2964.2 kJ/kg s = 7.3789 kJ/kg-K
44.86°C
15.25%
A 350 mm x 450 mm steam engine running at 280 rpm has a clearance steam condition of 2 MPa and 230°C and exits at 0.1 MPa. The steam consumption is 2000 kg/hr and mechanical efficiency is 85%. If indicated mean effective pressure is 600 kPa, determine brake thermal efficiency.
@ 2 MPa and 230°C: h1 = 2849.6 kJ/kg s1 = 6.4423 kJ/kg-K
@ 0.1 MPa: sf = 1.3026 kJ/kg-K hf = 417.46kJ/kg sfg = 6.0568 kJ/kg-K
hfg = 2258 kJ/kg hf2 = 417.46 kJ/kg
1373.60 kW
A steam turbine receives 5,000 kg/hr of steam at 5 MPa and 400°C and velocity of 30 m/s. It leaves the turbine at 0.006 MPa and 85% quality and velocity of 15 m/s. Radiation loss is 10,000 kJ/hr. Find the kW developed.
@5 MPa and 400°C: h1 = 3195.7 kJ/kg s1 = 6.6459 kJ/kg-K
@ 0.006 Mpa: hf = 151.53 kJ/kg hfg = 2415.9 kJ/kg
1,054.95 kJ/kg
A steam turbine with 85% stage efficiency receives steam at 7 MPa and 550°C and exhausts at 20 kPa. Determine the turbine work.
@ 7 MPa and 550°C: h1 = 3530.9 kJ/kg s1 = 6.9486 kJ/kg-K
@ 20 kPa (0.020 MPa): sf = 0.8320 kJ/kg-K hf = 251.40 kJ/kg
sfg = 7.0766 kJ/kg-K hfg = 2358.3 kJ/kg
96.96%
A steam turbine with 80% stage efficiency receives steam at 7 MPa and 550°C and exhausts at 20 kPa. Determine the quality at exhaust.
@ 7 MPa and 550°C: h1 = 3530.9 kJ/kg s1 = 6.9486 kJ/kg-K
@ 20 kPa (0.020 MPa): sf = 0.8320 kJ/kg-K hf = 251.40 kJ/kg
sfg = 7.0766 kJ/kg-K hfg = 2358.3 kJ/kg
2 wells
2,933 kg/s
A liquid dominated geothermal plant with a single flash separator receives water at 204°C. The separator pressure is 1.04 MPa. A direct contact condenser operates at 0.034 MPa. The turbine has a polytropic efficiency of 0.75. For cycle output of 60 MW, what is the mass flow rate of the well water in kg/s?
@ 204°C: hf = 870.51 kJ/kg
@ 1.04 MPa: hf = 770.38 kJ/kg hfg = 2009.2 kJ/kg hg = 2779.6 kJ/kg
sg = 6.5729 kJ/kg-K
@ 0.034 MPa: hf = 301.40 kJ/kg hfg = 2328.8 kJ/kg sf = 0.09793 kJ/kg-K
sfg = 6.7463 kJ/kg-K
25,714 kW
45%
14.64%
1.81 kg/s
P6.87/kW-hr
75.38%
835.57 kW
3.0 m
36.22 m
1,355.73 mm
80,080 kW-hrs
34,452 kW
0.0307
Water flows steadily with a velocity of 3.05 m/s in a horizontal pipe having a diameter of 25.24 cm. At one section of the pipe, the temperature and pressure of the water are 21°C and 689.3 kPa respectively. At a distance of 304.8 m downstream, the pressure is 516.9 kPa. What is the friction factor?
2.20 m
0.25 kPa
98 kPa
651.10 m
598 sacks