Vertical shell-and-tube heat exchanger and its block-proof method
A shell-and-tube heat exchanger and heat exchanger technology, applied in the field of polyolefin production, can solve problems such as single flow state of tube-side fluid, blockage of external circulation heat exchanger, large flow stagnation area, etc., to reduce deposition viscosity Possibility of knots, elimination of flow stagnation zones, effect of reducing particle stagnation zones
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Embodiment 1
[0034] Such as figure 1 As shown, in the traditional shell-and-tube heat exchanger, the fluid is introduced into the heat exchange tube from the fluid inlet at the lower tube box 6 through the lower tube sheet, and then from the other end of the heat exchange tube to the outlet of the upper tube box 7 through the upper tube sheet flow out of the heat exchanger. The flow state of the fluid in the tube side is relatively simple, and the degree of turbulence is relatively low. For the slurry heat exchange medium in the flow stagnation zone, after the slurry is introduced into the tube side of the heat exchanger and exchanged heat through the heat exchange tube, the temperature drop will cause the polymer to flow from the slurry to the heat exchange tube. Cohesion occurs in precipitation, especially in flow stagnation areas, such as between the parts of heat exchange tubes protruding from the tube sheet ( figure 1 Middle 1 area), the side wall area of the tube box ( figure 1 T...
Embodiment 2
[0040] see image 3 , the method of the present invention is used to set the internal component deflector in the upper tube box and or the lower tube box of the heat exchanger, and the slurry flows through the internal component deflector to form a flow along the axial direction of the heat exchanger and the radial direction of the heat exchanger. flow. The main parameters are shown in Table 2:
[0041] Table 2
[0042]
[0043] In the process of producing high-density polyethylene by slurry method, using the tubular heat exchanger of the present invention, the operating conditions are: the inlet temperature of the tube-side fluid is 78-85°C, the outlet temperature is 73-80°C, and the operating pressure is 0.23-0.70MPa , slurry flow rate 4m / s, slurry concentration 450g particles / L solvent, slurry particle density 0.950g / cm 3 , The particle size of the slurry is 100-200 mesh; the inlet temperature of the shell-side cooling water is 25-34°C, the outlet temperature is 55-65...
Embodiment 3
[0045] see Figure 4 , the method of the present invention is used to set the internal component deflector in the upper tube box and or the lower tube box of the heat exchanger, and the slurry flows through the internal component deflector to form a flow along the axial direction of the heat exchanger and the radial direction of the heat exchanger. flow. The main parameters are shown in Table 3:
[0046] table 3
[0047]
[0048] In the process of producing high-density polyethylene by slurry method, using the tubular heat exchanger of the present invention, the operating conditions are: the inlet temperature of the tube-side fluid is 78-85°C, the outlet temperature is 73-80°C, and the operating pressure is 0.23-0.70MPa , slurry flow rate 4.0m / s, slurry concentration 450g particles / L solvent, slurry particle density 0.950g / cm 3 , The particle size of the slurry is 100-200 mesh; the inlet temperature of the shell-side cooling water is 25-34°C, the outlet temperature is 55...
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