Transport Phenomena · Local conservation laws, constitutive fluxes, and scaling
A counterflow double-pipe heat exchanger cools 0.900 kg/s of a liquid process stream…
Problem
A counterflow double-pipe heat exchanger cools 0.900 kg/s of a liquid process stream from 150°C to a required 85.0°C using water entering at 20.0°C at 1.40 kg/s. Take the process-stream heat capacity as 2600 \(\mathrm{J\,kg^{-1}K^{-1}}\) and the water heat capacity as 4180 \(\mathrm{J\,kg^{-1}K^{-1}}\), both constant. The overall heat-transfer coefficient based on the available surface area is 310 \(\mathrm{W\,m^{-2}K^{-1}}\), and heat loss to the surroundings is negligible. Determine the water outlet temperature, verify numerically that counterflow terminal temperature differences remain positive, and calculate the required heat-transfer area using the log-mean temperature difference. The exchanger is assembled from identical 3.00 m modules, each providing 1.25 \(\mathrm{m^2}\) of area; determine the minimum integer number of modules required and the process-stream outlet temperature that this installed area would produce when both inlet temperatures and flow rates remain unchanged. For the installed-area calculation, use the counterflow effectiveness relation \(\varepsilon=[1-\exp(-NTU(1-C_r))]/[1-C_r\exp(-NTU(1-C_r))]\), with \(NTU=UA/C_{\min}\), \(C_r=C_{\min}/C_{\max}\), and \(Q=\varepsilon C_{\min}(T_{h,i}-T_{c,i})\).
Hint
First determine the required duty from the specified hot-stream temperature drop, then use it in the cold-stream energy balance.
Check your work
Work the problem yourself first. Then open it in Training to check your answer and read the full worked solution.
Create a free account to check your answer and see the solution. Create a free account.
More Transport Phenomena practice problems
- A Newtonian oil of density 860 kg/m^3 and viscosity 0.145 Pa s flows steadily through a…Local conservation laws, constitutive fluxes, and scaling
- An incompressible liquid approaches a porous flat surface with an accelerating external…Local conservation laws, constitutive fluxes, and scaling
- A spherical crystal of initial radius 6.00 mm and density 1200 kg/m^3 dissolves in a…Momentum transport and viscous flow
- A water film flows down a 0.500 m wide heated strip of length 2.00 mMomentum transport and viscous flow
- Hot water flows turbulently over one face of a flat plateMomentum transport and viscous flow
- A homogeneous half-space y>0 has thermal diffusivity α=1× 10^(-6) m^2/s and…Energy transport and convection-conduction coupling
- Two well-mixed compartments exchange a dilute solute through a membraneSpecies transport, diffusion, and convection
- A solute is carried down a straight circular tube of radius a=0.001 m by a fully…Species transport, diffusion, and convection
- A liquid element is exposed to a solute for a single contact time t_c=4 sBoundary layers and interfacial transfer coefficients