Forcible dredging type tubular heat exchange device for sewage or surface water
A technology of tubular heat exchange and surface water, which is applied to the types of heat exchangers, heat exchanger shells, indirect heat exchangers, etc. It can solve the problem of suspended solids and impurities in the flow channel, insufficient pressure bearing capacity of the plate structure, and casings. In order to solve the problems of large structural steel consumption and other problems, the effects of small water leakage accidents, no clogging, efficient heat exchange, and high pressure bearing capacity are achieved.
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specific Embodiment approach 1
[0034] Specific implementation mode one: as Figure 1-Figure 14 As shown, a forced dredging tubular heat exchange device for sewage or surface water in this embodiment includes a flow channel separation device 1, a plurality of heat exchange tubes 2, a shell 3, a left tube plate 4, a right tube plate 5, Left header 6, right header 7, left head 8, right head 9, multiple shell baffles 10, multiple shell inner diaphragms 11, multiple transverse diaphragm holes 12, multiple headers Baffle plate 13, multiple header dredging devices 14, multiple head baffles 15, header flange 16, head flange 17, sewage or surface water outlet 19, heat exchange medium inlet 20, heat exchange medium Outlet 21, shell side area 35, left tube side area 36, right tube side area 37, dredging area 38; the flow channel separation device 1 includes a flow channel separation shell 23, a plurality of flow channel separation plates 24, a plurality of separation Flow channel 25, multiple flow channel separatio...
specific Embodiment approach 2
[0035] Specific implementation mode two: as Figure 12 As shown in the specific embodiment 1, a forced dredging tubular heat exchange device for sewage or surface water, from the flow channel separation inlet 27 to the first flow channel separation inner port 26 to the last flow channel Separate the inner port 26, and gradually increase the distance from the flow channel separation short tube 29 in sequence, and the distance increased each time is 5mm-500mm.
specific Embodiment approach 3
[0036] Specific implementation mode three: as Figure 12 As shown, a forced-drainage tubular heat exchange device for sewage or surface water described in the second specific embodiment starts from the flow channel separation inlet 27 to the first flow channel separation port 26 to the last flow channel separation The distance from the inner port 26 to the flow channel separation short tube 29 increases gradually in sequence, and the distance increased each time is 50mm-200mm.
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