i.In a cyclic process heat transfer are +14.7 kJ, -25.2 kJ,
-3.56kJ and +31.5 kJ. What is the network for the cyclic process?
ii. Apply the steady flow energy equation to a Turbine and deduce an expression for work
A closed system consists of 1 kg of air which is initially at 1.5bar and 67°C. The volume doubles as the system undergoes a process according to the law PV1.2 = C. Find the work done, heat transfer and the change in entropy during this process. For air R= 0.287 kJ/kgK and γ = 1.4
find a homogeneous linear equation with real, constant coefficients that is satisfied by y=6+3xe^x–cos x
To determine and verify experimentally the law for total resistance (RT) of a series-parallel combination circuit.
2. To verify that the voltage across each leg in a parallel circuit is the same as the voltage across the parallel network.
Equipment
Project board 1 x 68Ω resistor
Multi-meter 1 x 82Ω resistor
Variable power supply 1 x 150Ω resistor
Wires 1 x 1k2 Ω resistor
1 x 10kΩ resistor
A system of forces 340 N, 760 N, 800 N, 600 N, 700 N and 500 N (in order) acting on
900 mm by 400 mm plate (with negligible thickness) is shown. Find the resultants with
respect to O.
Chemical P was fed into a CSTR reactor to react with an excess amount of chemical Q to produce chemical R. However, during the reaction, chemical S was also produced by conversion of chemical R. The reactions involve liquids and follow elementary rate law as follow:
P + Q → R (1)
R → S (2)
The reaction rate constant for chemical P for the first reaction was given as 4 dm3mol-1s-1, while the reaction rate constant for chemical R for the second reaction was given as 6 dm3mol-1s-1. The entering concentration of chemical P was 10 mol dm-3. Answer the following questions using the given information.
a) Write the net rate law for chemical P, R and S. (6 Marks)
b) Write the concentration of chemical P, R and S in terms of space time. (14 Marks)
As a new engineer in a company XZ, your boss has assigned you a project that is related to the removal of pollutant A in pharmaceutical wastewater. To achieve the objective of the project, you had conducted the experiment in a batch mode. The initial concentration of the pollutant A was set at 2.5 mol/dm3. The remaining concentration of the pollutant was identified using a UV-Vis. The complete experimental data obtained is tabulated in Table 1.
Table 1
t (hr) 5 10 15 20 25
A (mol/dm3) 1.95 1.65 1.15 0.88 0.60
a.Determine the removal rate of pollutant A by using numerical method. (15 Marks)
b.Is the removal time of 25 hours sufficiently enough to remove the pollutant A more than 90%? Justify your answer by using answer from (a). (5 Marks)
The irreversible gas phase reaction A + B --® 2C
is carried out in a PBR. The reaction rate is given as -rA = kCA. The feed is equal molar in A and B and the weight of the catalyst used is 15 kg.
Additional information FA0 = 100 mol/s
k = 1 dm3/kg.s CA0 = 1 mol/dm3
a = 0.064 kg-1
Determine the conversion exiting the reactor.
A first-order, irreversible liquid-phase reaction is taking place in a CSTR and 60% conversion is obtained. What is the minimum number of CSTR of the same size needed to place downstream in series to achieve 90% of total conversion.