Rework Example 15.6, assuming convective heat transfer to cooling water that surrounds the tube. Let the heat-transfer coefficient be \(h_{\mathrm{o}}=100 \mathrm{Btu} / \mathrm{ft}^{2}-\mathrm{hr}^{\circ} \mathrm{F}\).

Data From Example 15.6:-

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To assess a diabetic tubular reactor (with heat transfer at the walls), consider the assumption of a uniform wall temperature at 303.15 K (cooling water temperature). Compare the conversions, assuming: 1. Fully developed laminar flow with radial diffusion 2. Plug flow