CN220703305U - Foam separator - Google Patents

Foam separator Download PDF

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Publication number
CN220703305U
CN220703305U CN202322017825.1U CN202322017825U CN220703305U CN 220703305 U CN220703305 U CN 220703305U CN 202322017825 U CN202322017825 U CN 202322017825U CN 220703305 U CN220703305 U CN 220703305U
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tube
foam
ozone
disinfection
water
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CN202322017825.1U
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Chinese (zh)
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魏茂春
林献策
于乃衡
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Abstract

The utility model provides a foam separator, which comprises a disinfection tube and an ozone decomposition tube, wherein the bottom of the disinfection tube is communicated with the bottom of the ozone decomposition tube; the bottom of the disinfection tube is provided with an ozone bubble input mechanism, the lower layer of the ozone decomposition tube is provided with an air bubble input mechanism, the top of the disinfection tube and the top of the ozone decomposition tube are both provided with foam collecting cavities, the top of the disinfection tube is provided with a water inlet, the height of the disinfection tube is lower than that of the foam collecting cavities, and the foam collecting cavities are connected with a blow-down tube for discharging foam; the ozonolysis pipe is provided with a water outlet and is lower than the foam collecting cavity. The sewage in the culture pond is introduced into the disinfection pipe for disinfection through ozone, and then flows out through the ozone decomposition pipe, and air is introduced into the ozone decomposition pipe to decompose residual undissolved ozone in the disinfected sewage and further separate bubbles, so that not only is foam separation realized, but also ozone residues in water flow are reduced.

Description

Foam separator
Technical Field
The utility model relates to the technical field of aquaculture, in particular to a foam separator.
Background
In the aquaculture of aquatic economic animals, suspended particulate matter is produced and a portion of the organic matter is dissolved in the water. Farms typically use foam separators to separate impurities from the water, which separate the foam by air flotation. In the using process of the foam separator, ozone is generally added to achieve the disinfection and sterilization effects, and in addition, bubbles are generated after the ozone is decomposed, so that the air floatation effect is also generated. Air floatation principle: air floatation is to generate a large amount of fine bubbles in water, and the fine bubbles adhere to small suspended particles in the wastewater. The 'bubble particle' compound with the overall density smaller than that of water is formed, and the suspended particles rise to the water surface along with bubbles to form foam scum, so that suspended matters in the water can be separated.
The prior foam separator for aquaculture has certain defects when in use, and ozone residues are usually remained in the discharged water, so that the undigested ozone can be brought to a water outlet and sent to a biochemical filtration system, and microorganisms such as nitrifying bacteria in the biochemical filtration system can be killed.
Disclosure of Invention
In order to solve the problems, the utility model aims to provide the foam separator, sewage in a culture pond is introduced into a sterilizing pipe to be sterilized by ozone and then flows out through an ozone decomposing pipe, and air is introduced into the ozone decomposing pipe to decompose the residual undigested ozone in the water flow and further separate bubbles, so that the foam separation is realized, and the ozone residues in the water flow are reduced.
The utility model is realized by the following steps: a foam separator, comprising a disinfection tube and an ozone decomposition tube, wherein the bottom of the disinfection tube is communicated with the bottom of the ozone decomposition tube; the bottom of the disinfection tube is provided with an ozone bubble input mechanism, the lower layer of the ozone decomposition tube is provided with an air bubble input mechanism, the top of the disinfection tube and the top of the ozone decomposition tube are both provided with foam collecting cavities, the top of the disinfection tube is provided with a water inlet, the height of the disinfection tube is lower than that of the foam collecting cavities, and the foam collecting cavities are connected with a blow-down tube for discharging foam; the ozonolysis pipe is provided with a water outlet and is lower than the foam collecting cavity.
Preferably, the ozone bubble input mechanism comprises a first dissolved air pump, the inlet end of the first dissolved air pump is connected with a first water inlet pipe, a first air inlet pipe is connected to the first water inlet pipe, and the first air inlet pipe is connected with an ozone source; the outlet end of the first dissolved air pump is communicated with the bottom in the disinfection tube.
Preferably, a first diffusion baffle plate is arranged in the disinfection tube below the water inlet, the outlet end of the first dissolved air pump is connected with a first water outlet pipe, the outlet of the first water outlet pipe penetrates into the bottom in the disinfection tube, and the first diffusion baffle plate is positioned above the outlet of the first water outlet pipe; a plurality of diffusion holes are formed in the first diffusion partition plate in an array mode.
Preferably, the first air inlet pipe is further connected with an air source.
Preferably, the air bubble input mechanism comprises a second dissolved air pump, the inlet end of the second dissolved air pump is connected with a second water inlet pipe, the second water inlet pipe is connected with a second air inlet pipe, and the second air inlet pipe is connected with an air source; and the outlet end of the second dissolved air pump is communicated with the bottom of the ozone decomposition tube.
Preferably, a second diffusion baffle plate is arranged in the ozone decomposition tube below the water outlet, the outlet end of the second dissolved air pump is connected with a second water outlet pipe, the outlet of the second water outlet pipe penetrates into the bottom in the disinfection tube, and the second diffusion baffle plate is positioned above the outlet of the second water outlet pipe; and a plurality of diffusion holes are formed in the second diffusion baffle plate in an array mode.
Preferably, a foam collecting cup is arranged in the foam collecting cavity, and the upper end of the foam collecting cup is higher than the liquid level in the disinfection tube and the ozone decomposing tube; the lower end of the foam collecting cup is connected with the sewage draining pipe.
Preferably, the upper ends of the ozonolysis pipe and the disinfection pipe are both provided with a top cover.
Preferably, a concave arc-shaped connecting part is arranged between the ozone decomposition tube and the bottom of the disinfection tube, the arc-shaped connecting part is hollow, a drain outlet is arranged at the lowest point of the arc-shaped connecting part, and a drain valve is arranged at the drain outlet.
Preferably, a downward bent water outlet part is arranged at the water outlet.
The utility model has the beneficial effects that: compared with the prior art, the foam separator provided by the utility model has at least the following technical effects: 1. the disinfection pipe and the ozone decomposition pipe are communicated, sewage in the culture pond is introduced into the disinfection pipe to disinfect through ozone, and then flows out through the ozone decomposition pipe, and air is introduced into the ozone decomposition pipe to decompose residual non-decomposed ozone in water flow, so that foam separation is realized, ozone residues in water flow are reduced, and normal growth of aquatic products in the culture pond is guaranteed. 2. Ozone and air are uniformly dissolved in water through the air dissolving pump by the sterilizing pipe, and the conventional jet valve for products in the existing market has higher energy consumption, so that the ozone of the separator is more uniformly mixed, the energy consumption is lower, and the sterilizing effect is better. 3. The air is uniformly dissolved in the water by the dissolved air pump connected with the ozone decomposing pipe, so that ozone can be quickly decomposed, and residual undigested ozone is prevented from being brought to the water outlet; a large amount of air is dissolved in water to generate foam, so that the mixed air can be better combined with ozone in water flow in an ozone decomposition tube, ozone decomposition is thorough, and ozone residue in effluent is less. 4. By arranging the diffusion baffle plates in the disinfection tube and the ozone decomposition tube, bubbles containing oxygen or air can be uniformly distributed in the disinfection tube and the ozone decomposition tube, the contact area with water flow is increased, and better disinfection effect and ozone decomposition effect are achieved. 5. The foam is separated for the first time in the sterilizing tube, and is separated for the second time in the foam decomposing tube, and the foam separation effect is obviously stronger than that of the existing separator.
Drawings
Fig. 1 is a schematic view of the structure of a foam separator of the present utility model.
Fig. 2 is a schematic view of the structure of the first diffusion barrier of the present utility model.
Fig. 3 is an enlarged partial schematic view of fig. 1 a.
Reference numerals illustrate: 1-sterilizing pipes, 2-ozonolysis pipes, 3-ozone input mechanisms, 31-first dissolved air pumps, 32-first water inlet pipes, 33-first air inlet pipes, 34-first water outlet pipes, 4-air input mechanisms, 41-second dissolved air pumps, 42-second water inlet pipes, 43-second air inlet pipes, 44-second water outlet pipes, 5-foam collecting cavities, 6-water inlets, 7-blow-down pipes, 8-water outlets, 9-first diffusion baffle plates, 10-second diffusion baffle plates, 11-foam collecting cups, 12-top covers, 13-arc-shaped connecting parts and 14-drainage valves.
Detailed Description
The utility model will be further described with reference to the drawings and specific examples.
Referring to fig. 1 to 3, a foam separator includes a sterilizing pipe 1 and an ozone decomposing pipe 2, wherein the sterilizing pipe 1 is communicated with the bottom of the ozone decomposing pipe 2; the lower layer of the disinfection tube 1 is provided with an ozone bubble input mechanism 3, the bottom of the ozone decomposition tube 2 is provided with an air bubble input mechanism 4, the tops of the disinfection tube 1 and the ozone decomposition tube 2 are respectively provided with a foam collecting cavity 5, the top of the disinfection tube 1 is provided with a water inlet 6, the height of the water inlet is lower than that of the foam collecting cavity 5, and the foam collecting cavity 5 is connected with a blow-down pipe 7 for discharging foam; the ozonolysis pipe 2 is provided with a water outlet 8 which is lower than the foam collecting cavity 5. The disinfection pipe 1 and the ozonolysis pipe 2 are communicated, sewage in the culture pond is introduced into the disinfection pipe 1 to be disinfected by ozone, and then flows out through the ozonolysis pipe 2, and air is introduced into the ozonolysis pipe 2 to decompose residual non-decomposed ozone in water flow, so that foam separation is realized, ozone residues in water flow are reduced, and normal growth of aquatic products in the culture pond is ensured. The communicated disinfection tube 1 and the ozone decomposition tube 2 are communicated to form a U-shaped tube, the water levels at the two sides are the same, foam in water flow is carried up by the air bubbles input by the ozone bubble input mechanism 3 and the air bubble input mechanism 4 to float gradually until floating in the foam collecting cavity 5, and foam overflows through the blow-off tube 7 along with the gradual increase of foam, so that foam separation is realized.
Referring to fig. 1, preferably, the ozone bubble input mechanism 3 includes a first dissolved air pump 31, an inlet end of the first dissolved air pump 31 is connected with a first water inlet pipe 32, a first air inlet pipe 33 is connected to the first water inlet pipe 32, and the first air inlet pipe 33 is connected to an ozone source (such as an ozone tank); the outlet end of the first dissolved air pump 31 is communicated with the bottom in the disinfection tube 1. Because the water flow speed of the first water inlet pipe 32 is high, the first water inlet pipe 32 forms negative pressure to suck ozone or air from the first air inlet pipe 33 (Venturi effect), so that the ozone can be sucked into the first water inlet pipe 32 from an ozone source to be mixed with water, and then the ozone is scattered by the blades of the first dissolved air pump 31 to be more uniformly and finely mixed in the water, and then the water is introduced into the disinfection pipe 1 to disinfect and separate foam from water flow discharged from a cultivation pond.
Referring to fig. 1 and 3, preferably, a first diffusion baffle plate 9 is disposed below the water inlet 6 in the disinfection tube 1, an outlet end of the first dissolved air pump 31 is connected with a first water outlet pipe 34, an outlet of the first water outlet pipe 34 penetrates into the bottom of the disinfection tube 1, and the first diffusion baffle plate 9 is disposed above an outlet of the first water outlet pipe 34; a plurality of diffusion holes are formed in the first diffusion partition 9 in an array. After the clean water which is rich in bubbles and is led out from the outlet end is led in, the bubbles float in the disinfection tube 1 more uniformly under the guidance of the diffusion baffle plates.
Referring to fig. 1, preferably, the first air inlet pipe 33 is further connected to an air source (e.g. directly sucking air from outside the first air inlet pipe). The air bubbles are increased, so that the separation effect of the foam and the water flow is better. For controlling the ingress of gas. The first air inlet pipe 33 is preferably connected with a three-way pipe, one end of the three-way pipe is connected with the first air inlet pipe 33, the other two ends of the three-way pipe are respectively connected with a pipeline for connecting an air source and a pipeline for connecting an ozone source, and electromagnetic valves are respectively arranged on the corresponding pipelines and used for controlling air to flow into the first air inlet pipe 33.
Referring to fig. 1 to 3, preferably, the air bubble input mechanism 4 includes a second dissolved air pump 41, an inlet end of the second dissolved air pump 41 is connected with a second water inlet pipe 42, a second air inlet pipe 43 is connected to the second water inlet pipe 42, and the second air inlet pipe 43 is connected with an air source; the outlet end of the second dissolved air pump 41 is communicated with the bottom of the ozone decomposing tube 2. Because the second water inlet pipe 42 is fast in water flow speed, the second water inlet pipe 42 forms negative pressure to suck air from the second air inlet pipe 43 (Venturi effect), the air can be sucked from the second air inlet pipe 43 to the second water inlet pipe 42 to be mixed with water, the air is scattered through the blades of the second dissolved air pump 41 to be more uniformly and finely mixed with water, and then the air is introduced into the ozone decomposing tube 2 to carry out ozone decomposition and further foam separation on the water flow disinfected by the disinfection tube 1.
Referring to fig. 1 to 2, preferably, a second diffusion baffle 10 is disposed below the water outlet 8 in the ozone decomposing tube 2, an outlet end of the second dissolved air pump 41 is connected with a second water outlet pipe 44, an outlet of the second water outlet pipe 44 penetrates into the bottom of the sterilizing tube 1, and the second diffusion baffle is disposed above an outlet of the second water outlet pipe 44; the second diffusion partition 10 is provided with a plurality of diffusion holes in an array. The same structure as the first diffusion barrier 9.
Referring to fig. 1 and 3, preferably, a foam collecting cup 11 is disposed in the foam collecting chamber 5, and the upper end of the foam collecting cup 11 is higher than the liquid level in the sterilizing tube 1 and the ozonolysis tube 2; the lower end of the foam collecting cup 11 is connected with the blow-down pipe 7. Along with the gradual accumulation of the foam in the foam collecting cavity 5, as only the drain pipe 7 connected with the bottom of the foam collecting cup 11 can be discharged, the foam can be extruded into the drain pipe 7 and can be discharged along the drain pipe 7, and the height h=2-10 mm higher than the liquid level on the upper surface of the foam collecting cup can flow into the collecting cup to be discharged when the foam is generated. Other manufacturer products in the market mainly flow out from the upper pipeline, so that the total height of the foam separator can be reduced, and the discharge resistance of discharged foam is reduced.
Referring to fig. 1, preferably, the ozonolysis pipe 2 and the sterilizing pipe 1 are provided with a top cover 12 at their upper ends. The foam is prevented from overflowing from the top ends of the decomposition tube and the sterilization tube 1, so that the foam must be discharged from the drain tube 7.
Referring to fig. 1, preferably, a concave arc-shaped connecting portion 13 is disposed between the ozone decomposing tube 2 and the bottom of the sterilizing tube 1, the arc-shaped connecting portion 13 is hollow, a drain outlet is disposed at the lowest point of the arc-shaped connecting portion 13, and a drain valve 14 is disposed at the drain outlet. It should be noted that the outlet heights of the first water outlet pipe 34 and the second water outlet pipe 44 are higher than the highest point of the concave part under the arc-shaped connecting part, so that bubbles are prevented from running from the sterilizing tube 1 to the ozone decomposing tube 2. The arc-shaped connecting part 13 at the bottom is in a U-shaped pipe shape, so that impurities are not easy to precipitate and the cleaning is easy. Opening the drain valve 14 can drain the impurities deposited at the bottom of the arc-shaped connection portion 13.
Referring to fig. 1, preferably, the water outlet 8 is provided with a downward bent water outlet. So as to facilitate the rising of the air bubbles and prevent the air bubbles from flowing to the water outlet 8.
Referring to fig. 1, the water inlet 6 is higher than the water outlet 8, so as to facilitate the water outlet after treatment.
The utility model has the following working principle:
the sewage discharged from the culture pond is introduced into the disinfection tube 1, at the moment, the first dissolved air pump 31 works to pump clean water flow mixed with ozone and air into the disinfection tube 1, the dense ozone-rich water flow is fully mixed with the sewage in the disinfection tube 1, so that disinfection can be performed, (at the moment, foam in the sewage can be driven to be carried up due to light upward floating of the density of the air bubbles, and the foam is sent into the foam collecting cavity 5 on the disinfection tube 1, and can only be extruded into the foam collecting cup 11 and then discharged through the blow-down tube 7 along with the gradual filling of the collecting cavity); the disinfected sewage enters the ozone decomposing tube 2 through the arc-shaped connecting part 13, the ozone decomposing tube 2 pumps water flow rich in air bubbles through the second dissolved air pump 41, the bubbles in the water flow are fully contacted with the sewage, the residual undigested ozone in the disinfected sewage can be decomposed, the ozone residual in the sewage is reduced (meanwhile, rising bubbles can further take away residual foam in the water flow to float, the residual foam is concentrated in the foam collecting cavity 5 of the ozone decomposing tube 2, the foam is gradually accumulated to exceed the storage capacity of the collecting cavity, the foam can be extruded into the foam collecting cup 11 in the foam collecting cavity and then discharged through the blow-down pipe 7), and the normal growth of aquatic products in the culture pond is further ensured; the foam in the sewage is separated in two stages, so that a better foam separation effect can be achieved, the foam of the sewage treated by the separator is less, and the residual ozone is close to 0.
The points to be described are: first, in the description of the present application, it should be noted that, unless otherwise specified and defined, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be mechanical or electrical, or may be a direct connection between two elements, and "upper," "lower," "left," "right," etc. are merely used to indicate relative positional relationships, which may be changed when the absolute position of the object being described is changed.
Secondly: in the drawings of the disclosed embodiments, only the structures related to the embodiments of the present disclosure are referred to, and other structures may refer to the general design, so that the same embodiment and different embodiments of the present disclosure may be combined with each other without conflict.
Finally, the above description is only a preferred embodiment of the present utility model, and the scope of the present utility model is not limited to the above examples, but all technical solutions belonging to the concept of the present utility model are within the scope of the present utility model.
It should be noted that modifications and adaptations to the present utility model may occur to one skilled in the art without departing from the principles of the present utility model and are intended to be within the scope of the present utility model.

Claims (10)

1. A foam separator, characterized by: the device comprises a disinfection tube and an ozone decomposition tube, wherein the bottom of the disinfection tube is communicated with the bottom of the ozone decomposition tube; the bottom of the disinfection tube is provided with an ozone bubble input mechanism, the lower layer of the ozone decomposition tube is provided with an air bubble input mechanism, the top of the disinfection tube and the top of the ozone decomposition tube are both provided with foam collecting cavities, the top of the disinfection tube is provided with a water inlet, the height of the disinfection tube is lower than that of the foam collecting cavities, and the foam collecting cavities are connected with a blow-down tube for discharging foam; the ozonolysis pipe is provided with a water outlet and is lower than the foam collecting cavity.
2. A foam separator as claimed in claim 1, wherein: the ozone bubble input mechanism comprises a first dissolved air pump, the inlet end of the first dissolved air pump is connected with a first water inlet pipe, a first air inlet pipe is connected to the first water inlet pipe, and the first air inlet pipe is connected with an ozone source; the outlet end of the first dissolved air pump is communicated with the bottom in the disinfection tube.
3. A foam separator as claimed in claim 2, wherein: a first diffusion baffle plate is arranged below the water inlet in the disinfection tube, the outlet end of the first dissolved air pump is connected with a first water outlet tube, the outlet of the first water outlet tube penetrates into the bottom in the disinfection tube, and the first diffusion baffle plate is arranged above the outlet of the first water outlet tube; a plurality of diffusion holes are formed in the first diffusion partition plate in an array mode.
4. A foam separator as claimed in claim 2, wherein: the first air inlet pipe is also connected with an air source.
5. A foam separator as claimed in claim 1, wherein: the air bubble input mechanism comprises a second dissolved air pump, the inlet end of the second dissolved air pump is connected with a second water inlet pipe, a second air inlet pipe is connected to the second water inlet pipe, and the second air inlet pipe is connected with an air source; and the outlet end of the second dissolved air pump is communicated with the bottom of the ozone decomposition tube.
6. A foam separator as claimed in claim 5, wherein: a second diffusion baffle plate is arranged below the water outlet in the ozone decomposition tube, the outlet end of the second dissolved air pump is connected with a second water outlet tube, the outlet of the second water outlet tube penetrates into the bottom in the disinfection tube, and the second diffusion baffle plate is positioned above the outlet of the second water outlet tube; and a plurality of diffusion holes are formed in the second diffusion baffle plate in an array mode.
7. A foam separator as claimed in claim 1, wherein: a foam collecting cup is arranged in the foam collecting cavity, and the upper end of the foam collecting cup is higher than the liquid level in the disinfection tube and the ozone decomposition tube; the lower end of the foam collecting cup is connected with the sewage draining pipe.
8. A foam separator as claimed in claim 1, wherein: the upper ends of the ozone decomposition tube and the disinfection tube are both provided with a top cover.
9. A foam separator as claimed in claim 1, wherein: the ozone decomposing tube is characterized in that a concave arc-shaped connecting part is arranged between the ozone decomposing tube and the bottom of the sterilizing tube, the arc-shaped connecting part is hollow, a water outlet is formed in the lowest point of the arc-shaped connecting part, and a water draining valve is arranged at the water outlet.
10. A foam separator as claimed in claim 1, wherein: the water outlet is provided with a downward bent water outlet part.
CN202322017825.1U 2023-07-30 2023-07-30 Foam separator Active CN220703305U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202322017825.1U CN220703305U (en) 2023-07-30 2023-07-30 Foam separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202322017825.1U CN220703305U (en) 2023-07-30 2023-07-30 Foam separator

Publications (1)

Publication Number Publication Date
CN220703305U true CN220703305U (en) 2024-04-02

Family

ID=90442901

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202322017825.1U Active CN220703305U (en) 2023-07-30 2023-07-30 Foam separator

Country Status (1)

Country Link
CN (1) CN220703305U (en)

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