Step 1: Find the Temperature Gradient in Air
Taking the derivative of the temperature profile:
$$\frac{dT}{dy} = \frac{d}{dy}(300 + 200e^{-5y})$$
$$\frac{dT}{dy} = 200 \times (-5) \times e^{-5y}$$
$$\frac{dT}{dy} = -1000e^{-5y}$$
Step 2: Evaluate Temperature Gradient in Air at y = 0
At the surface ($y = 0$):
$$\left(\frac{dT}{dy}\right)_{air, y=0} = -1000e^{0} = -1000 \text{ K/m}$$
Step 3: Apply Heat Flux Continuity at the Interface
At the interface between the slab and air, the heat flux must be continuous (no heat generation or accumulation at the interface):
$$q_{slab} = q_{air}$$
$$-k_{slab}\left(\frac{dT}{dy}\right){slab} = -k{air}\left(\frac{dT}{dy}\right)_{air}$$
Step 4: Calculate Temperature Gradient in Slab at y = 0
$$k_{slab}\left(\frac{dT}{dy}\right){slab, y=0} = k{air}\left(\frac{dT}{dy}\right)_{air, y=0}$$
$$100 \times \left(\frac{dT}{dy}\right)_{slab, y=0} = 1.0 \times (-1000)$$
$$\left(\frac{dT}{dy}\right)_{slab, y=0} = \frac{-1000}{100} = -10 \text{ K/m}$$
Step 5: Find the Magnitude
$$\left|\frac{dT}{dy}\right|_{slab, y=0} = |-10| = 10 \text{ K/m}$$
Answer: The magnitude of temperature gradient within the slab at y = 0 is 10 K/m.
Consider two identical tanks with a bottom hole of diameter \( d \). One tank is filled with water and the other tank is filled with engine oil. The height of the fluid column \( h \) is the same in both cases. The fluid exit velocity in the two tanks are \( V_1 \) and \( V_2 \). Neglecting all losses, which one of the following options is correct?
