In: Mechanical Engineering
Determine the chimney height required to preserve design flow in a natural recirculation boiling water reactor channel with the following characteristics:
System pressure: 7.136 MPa
Reactor height 1.83 m
Feedwater temperature 260 Celsius
Combined pressure in losses in the channel, chimney, and downcomer: 1344.5 Pa
Average channel density in the core: 642.9 kg / m^3
Two-phase friction losses in the chimney 137.9 Pa
Friction losses in the downcomer: 68.9 Pa
Friction drop in channel: 606.7 Pa
Average exit void fraction: 44%
Feedwater added near the top of chimney
Ans. Calculate 1/[S] and 1/Vo. Make LB Plot using excel or other similar software.
# Determination of Vmax and Km using LB Plot”
Lineweaver-Burk plot gives an equation in from of y = mx + c
where, y = 1/ Vo, x = 1/ [S],
Intercept, c = 1/ Vmax ,
Slope, m = Km/ Vmax
#A. Enzyme kinetics at I = 0.0 mM [y = 0.4836x + 0.1951]:
Vmax = 1 / c = 1 / 0.1951 = 5.1256
Hence, Vmax = 5.1256 mmol L-1 min-1
Now,
Km = m x Vmax = 0.4836 x 5.1256 = 2.4787
Hence, Km = 2.4787 mM
#B. Vmax,app and Km,aapp in presence of inhibitor is calculated similarly, the result is tabulated in excel sheet.
At [I] = 3.0 mM; Vmax,app = 5.1335 mmol L-1min-1
At [I] = 5.0 mM; Vmax,app = 4.9727 mmol L-1min-1
#C. At [I] = 3.0 mM; Km,app = 3.8773 mM
At [I] = 5.0 mM; Km,app = 4.9632 mM
#D. Type of Inhibitor: Note that the Vmax remains almost constant whereas Km increases in presence of inhibitor. It is the characteristic of a competitive inhibitor. So, the inhibitor is a competitive inhibitor.
# At [I] = 3.0 mM
KI of completive inhibition is given by-
KI = [I] / [(Km,app / Km) – 1] - equation 1
Putting the values in equation 1-
KI = 3 mM / [(3.8773 mM / 2.4787 mM) - 1]
Or, KI = 3 mM / (1.564 - 1)
Or, KI = 3 mM / 0.564
Hence, KI = 5.319 mM
# At [I] = 5.0 mM
Putting the values in equation 1-
KI = 5 mM / [(4.9632 mM / 2.4787 mM) - 1]
Or, KI = 5 mM / 1.00
Hence, KI = 5.00 mM