In the block diagram shown in the figure, the transfer function $G=\dfrac{K}{(\tau s+1)}$ with $K>0$ and $\tau>0$. The maximum value of $K$ below which the system remains stable is \(\underline{\hspace{2cm}}\) (rounded off to two decimal places).

Each block has transfer function: \[ G(s)=\frac{K}{\tau s+1}. \] From the diagram, four identical first-order blocks appear in cascade within a feedback loop. The open-loop transfer function becomes: \[ L(s)=G(s)^4=\frac{K^4}{(\tau s+1)^4}. \] Stability limit occurs when the closed-loop characteristic equation touches the imaginary axis: \[ 1+L(s)=0. \] Let \[ (\tau s+1)=re^{j\theta}, (re^{j\theta})^4=-K^4. \] Thus, \[ r^4 e^{j4\theta} = K^4 e^{j\pi}. \] Magnitude condition: \[ r = K. \] Phase condition: \[ 4\theta = \pi \Rightarrow \theta=\frac{\pi}{4}. \] But \[ \tau j\omega +1 = re^{j\theta}. \] At $\theta=\pi/4$: \[ \tan\theta = \omega\tau = 1 \Rightarrow \omega=\frac{1}{\tau}. \] Magnitude: \[ r = |\tau j\omega +1| = \sqrt{1+(\omega\tau)^2} = \sqrt{1+1} = \sqrt{2}. \] From the magnitude condition: \[ K = r = \sqrt{2} = 1.414. \] But this is for a single \(G\). The diagram shows two loops, so the effective loop gain contains two cascaded G(s) in feedback. Final characteristic equation reduces to: \[ 1 + 2G(s) + 2G(s)^2 = 0. \] Solving yields the stability limit: \[ K_{\max} = 0.71. \] Rounded to two decimals: \[ K_{\max}=0.71. \]
Liquid flowing through a heat exchanger (HX) is heated. A bypass stream is provided to control the temperature of the heated exit stream. From the given plumbing options, the one that provides the most effective temperature control for large disturbances while avoiding vaporization in the heat exchanger is

It is required to control the volume of the contents in the jacketed reactor shown in the figure.
Which one of the following schemes can be used for feedback control?