A louver-shaped baffle fixed tube-sheet heat exchanger and its processing and installation method
A technology of fixed tube-sheet type and installation method, applied in the direction of indirect heat exchanger, heat exchanger type, heat exchanger shell, etc., can solve the problem of strict shell-side flow velocity and tube bundle layout, complex structure, manufacturing and installation, and power equipment power Large and other problems, to achieve the effect of good anti-fouling performance of the equipment, easy assembly, and reduced pump power
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Embodiment approach 1
[0045] See figure 1 Shown: the louver-shaped baffle fixed tube sheet heat exchanger of the present invention includes a tube side inlet tube box 1, a shell 2, a heat exchange tube bundle 3, a tube side fluid inlet 4, a tube side fluid outlet 5, and a shell side fluid Inlet 6, shell side fluid outlet 7, tube side outlet tube box 8, louver-shaped baffle support structure 9, tube sheet 10. The tube boxes are located at both ends of the heat exchanger, and the tube side fluid inlet 4 and the tube side fluid outlet 5 are welded to the tube side inlet tube box 1 and the tube side outlet tube box 8 respectively. The shell-side fluid inlet 6 and the shell-side fluid outlet 7 are welded to the shell 2 and the positions are shown in the figure. The heat exchange tube bundle 3 is inserted into the louver-shaped baffle support structure 9, and both ends are welded and fixed on the tube sheet 10. The louver-shaped baffle support structure 9 is welded to the shell 2 at equal intervals acco...
Embodiment approach 2
[0057] The width of each blade is 25% of the diameter of the shell, the inclination angle θ is 80°, and its thickness is determined by the unsupported span of the heat exchange tube and the nominal diameter of the shell, and the range is 22mm. Others are the same as in embodiment 1.
Embodiment approach 3
[0059] The width of each blade is 20% of the diameter of the shell, the inclination angle θ is 10°, and its thickness is determined by the unsupported span of the heat exchange tube and the nominal diameter of the shell, and the range is 3mm. Others are the same as in embodiment 1.
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