High efficiency wet desulfuration and dust-removing device
A technology of wet desulfurization and dust removal device, which is applied to the separation of dispersed particles, chemical instruments and methods, and the use of liquid separation agents, etc., can solve the problems of large drop of fluid resistance in the tower, less contact probability, and short contact time, and achieve desulfurization and dust removal. The effect of sufficient, full gas-liquid mixing, and complete contact reaction
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Embodiment 1
[0015] Embodiment 1. The high-efficiency wet desulfurization and dust removal device of this embodiment can be obtained from figure 1 , figure 2 with Figure 5 , Image 6 As can be seen in the figure, it includes an upright main tower 1 with an inner tower 2 in its center, a flue gas outlet pipe 11 is arranged at the top of the main tower, and a tangential flue gas inlet pipe 3 and gray water and desulfurization pipes are arranged at the bottom. The outlet pipe 12 of the slag, the upper and lower parts of the tower wall are respectively provided with a group of tangential liquid spray pipes 8, and the inner wall of the main tower 1 above the top of the inner tower 2 has a water retaining ring 10, and the main tower and the inner tower The walls of the inner tower are respectively provided with an inner convex ring 5 and a conical protrusion 5' that can make the fluid shrink to the center suddenly and then gradually expand upwards, and an overflow device 7 for the liquid med...
Embodiment 2
[0017] Embodiment 2. This embodiment can be obtained from figure 1Seen in, it differs from embodiment 1 in that: the top of inner tower 2 can also be provided with dehydrator 9, and this dehydrator is a disc that is fixed on the top of inner tower and its diameter is greater than inner tower diameter. In this example, the dehydrator is installed on the top of the inner tower loam cake 2a. Together with the water retaining ring 10, it intercepts liquid droplets and solids from different radial positions in the main tower, and drops down by their own weight. The slag is discharged from the outlet pipe 12, while the flue gas is discharged from the flue gas outlet pipe 11 upwards by inertia.
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