Two-stage cascade high-humidity smoke condensing and spraying heat exchange method and device
A flue gas condensing and spraying device technology, applied in direct contact heat exchangers, heat exchanger types, water shower coolers, etc. quantity etc.
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specific Embodiment 2
[0028] The specific embodiment 2 of the present invention is as follows: the water-air diversion device 7 is not provided in the spray tower of this embodiment, that is, the part forms an empty section structure, and no water-air diversion device communicating with the low-temperature process water outlet G is no longer provided at this time 7, the low-temperature process water that falls to the structure of the empty section continues to descend and enters the high-temperature heat exchange section 5 after passing through the spray device 6 in the high-temperature section. Except above-mentioned difference, all the other parts are with specific embodiment 1.
specific Embodiment 3
[0029] The specific embodiment 3 of the present invention is as follows: the high-temperature heat exchange section 5 and the low-temperature heat exchange section 8 of this embodiment are vertically arranged counter-current heat exchange structures composed of air and spray water, wherein no filler is provided inside and an empty section structure is adopted. The high-temperature section spray device 6 and the low-temperature section spray device 9 are composed of N-layer spray structures, where N>1; the diameter of the outlet section 11 is significantly smaller than that of the lower low-temperature heat exchange area. Except above-mentioned difference, all the other parts are with specific embodiment 1.
specific Embodiment 4
[0030] The specific embodiment 4 of the present invention is as follows: the water-air diversion device 7 is not provided in the spray tower of this embodiment, that is, the part forms an empty section structure, and no water-air diversion device communicated with the low-temperature process water outlet G is no longer provided at this time 7, the low-temperature process water that falls to the structure of the empty section continues to descend and enters the high-temperature heat exchange section 5 after passing through the spray device 6 in the high-temperature section. Except above-mentioned difference, all the other parts are with specific embodiment 3.
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