Water recovery system for use in confined spaces
US-2015353401-A1 · Dec 10, 2015 · US
US11535540B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11535540-B2 |
| Application number | US-201816957471-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 4, 2018 |
| Priority date | Dec 27, 2017 |
| Publication date | Dec 27, 2022 |
| Grant date | Dec 27, 2022 |
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The invention discloses a double-tank oxidation pond for evaluating catalytic ozonation efficiency, comprising detachable tank bodies made of organic glass, movable ozone aeration pipes and sampling holes. Each tank body has three sections. The height of ozone aeration tube and the number of the holes can be adjusted. The holes are distributed at different positions of the tank bodies for real-time in-situ sampling. It is easy to observe the distribution profile of the gas, liquid and solid phases in the tank bodies. The square double-tank structure is similar to actual production process, and thus the experimental data is easy for computer simulation to enlarge to the actual production process. The size of the ozone aeration pipe and the position of holes in the tank can be adjusted to evaluate the catalytic ozonation effect of sewage treated by different aeration ways and aeration heights.
Opening claim text (preview).
What is claimed is: 1. A double-tank oxidation reactor for evaluating catalytic ozonation efficiency, comprising: a base; a tank body A and a tank body B which are independently fixed and spaced side by side on the base, wherein sampling holes are opened on the tank body A and the tank body B respectively, and gas inlet pipe openings are opened on a wall of each of the tank body A and the tank body B; water inlets provided on the tank body A; water inlet pipes, which are detachably connected to the water inlets; water outlets provided on the tank body B; water outlet pipes connected to the water outlets; sampling needles, which are removably plugged to the sampling holes; ozone aeration pipes, which are detachably inserted to the gas inlet pipe openings; and a communication pipe connected between the tank body A and the tank body B; wherein each of the tank body A and the tank body B is provided with a filler supported overflow sieve plate at an inner lower end thereof. 2. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the tank body A is formed by connecting three tank body sections in the vertical direction by a first flange, the tank body B is formed by connecting three tank body sections in the vertical direction by a second flange, the tank body A has a cross-sectional area as twice as that of the tank body B, the tank body A and the tank body B has the same height and are connected by an upper beam and a lower beam. 3. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the tank body A and the tank body B are both made of organic glass, and a drain pipe having a first valve is provided at the bottom of the tank body A. 4. A double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein three water inlets are distributed and spaced on the upper, middle and lower parts of the tank body A, and three water outlets are distributed and spaced on the upper, middle and lower parts of the tank body B, and the water outlet pipe is provided with a second valve. 5. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the sampling holes on the tank body A are evenly distributed and spaced on the middle portions of the front face and the side face of the tank body A from bottom to top, and the sampling holes on the tank body B are evenly distributed and spaced on the left edge and the middle portion of the front face of the tank body B from bottom to top. 6. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 5 , wherein the sampling hole comprises a stepped round holes, a silicone ball with a pinhole and a third flange; the silicone ball with a pinhole is placed on the stepped round hole and is pressed by the third flange. 7. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the ozone aeration pipe is supported by four supporting blocks, each supporting block is fixedly connected to a screw hole in the tank body via a screw. 8. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the ozone aeration pipe comprises an gas intake manifold and five branch pipes, the gas intake manifold is detachably inserted in the gas inlet pipe opening, the gas intake manifold and the gas inlet pipe opening are sealed by a first O-ring, and the five branch pipes are connected to each other in a shape of the Chinese character “ H”, wherein one of the five branch pipes is connected to the gas intake manifold and sealed by a second O-ring, and the five branch pipes have at least four aeration holes which are oriented downwards and at an angle of 45° to the vertical direction. 9. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the communication pipe is connected between the bottoms of the tank body A and the tank body B and is provided with a third valve. 10. The double-tank oxidation reactor for evaluating catalytic ozonation efficiency according to claim 1 , wherein the filler supported overflow sieve plate has elongated slots thereon, and each filler supported overflow sieve plate is supported in the tank body A and the tank body B by uprights at the four corners thereof.
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