CN210711094U - Sewage purification device - Google Patents
Sewage purification device Download PDFInfo
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- CN210711094U CN210711094U CN201920511085.8U CN201920511085U CN210711094U CN 210711094 U CN210711094 U CN 210711094U CN 201920511085 U CN201920511085 U CN 201920511085U CN 210711094 U CN210711094 U CN 210711094U
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- Prior art keywords
- water
- adsorber
- centrifugal
- sewage
- water molecule
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- 239000010865 sewage Substances 0.000 title claims abstract description 48
- 238000000746 purification Methods 0.000 title claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 162
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000003795 desorption Methods 0.000 claims abstract description 19
- 239000008213 purified water Substances 0.000 claims abstract description 13
- 239000006096 absorbing agent Substances 0.000 abstract description 9
- 239000002384 drinking water standard Substances 0.000 abstract description 4
- 239000013505 freshwater Substances 0.000 abstract description 4
- 238000003911 water pollution Methods 0.000 abstract description 4
- 238000001179 sorption measurement Methods 0.000 description 33
- 239000000463 material Substances 0.000 description 29
- 238000000034 method Methods 0.000 description 22
- 239000000126 substance Substances 0.000 description 11
- 238000000889 atomisation Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 229910001385 heavy metal Inorganic materials 0.000 description 8
- 239000012535 impurity Substances 0.000 description 6
- 230000001954 sterilising effect Effects 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000000741 silica gel Substances 0.000 description 4
- 229910002027 silica gel Inorganic materials 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 3
- 238000010170 biological method Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000000053 physical method Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000002131 composite material Substances 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007102 metabolic function Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model provides a sewage purification device, which comprises an ultrasonic atomizer, a water molecule absorber, a high-speed centrifugal desorption device, a centrifugal water collecting cylinder, an ozone generator and a water purification tank; the inlet end of the ultrasonic atomizer is connected with a sewage source, the outlet end of the ultrasonic atomizer is connected to the water molecule adsorber through a pipeline, and the water molecule adsorber is arranged on the periphery of the high-speed centrifugal desorption device and is driven to rotate by the high-speed centrifugal desorption device; the centrifugal water collecting cylinder is arranged on the periphery of the water molecule adsorber and is connected with the purified water tank; the ozone generator is connected with the water molecule adsorber through a pipeline. Through the utility model provides a sewage purification device can realize the deep purification at water source, and the water after the purification can reach the drinking water standard, can solve global water crisis and universal water pollution, improves the fresh water resource capacity of earth's surface.
Description
Technical Field
The utility model relates to a sewage purification device belongs to sewage purification technical field.
Background
At present, sewage purification can be classified into a physical method, a biological method and a chemical method according to its effect:
the first method comprises the following physical methods: mainly utilizes physical action to separate non-soluble substances in the sewage, and does not change chemical properties in the treatment process. Gravity separation, centrifugal separation, reverse osmosis, air flotation, etc. are commonly used.
The method can not completely remove pollutants and impurities in water, particularly micro particles, and is a simple primary purification method. The principle of the method lies in extracting or filtering large particles in the sewage to realize water source purification.
II, biological method: by utilizing the metabolism function of microorganisms, the organic matters in a dissolved or colloidal state in the sewage are decomposed and oxidized into stable inorganic substances, so that the sewage is purified. Commonly used are an activated sludge process and a biofilm process. The biological method has higher treatment degree than the physical method. However, this method has no effect on heavy metals in sewage, and only removes inorganic substances in water, and cannot achieve deep purification and complete purification of water sources.
Thirdly, a chemical method: the method is a method for treating or recovering dissolved substances or colloidal substances of sewage by utilizing chemical reaction, and is mainly used for industrial wastewater. As the method, coagulation, neutralization, redox, ion exchange, etc. are generally used. The chemical treatment method has good treatment effect and high cost, is mainly used for effluent after biochemical treatment and further treatment, and improves the effluent quality. This method is costly and remains chemically present in the water after treatment and is not useful for drinking.
The existing sewage treatment methods can not realize the deep purification of water sources, so a new sewage purification device needs to be designed to overcome the problems.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome prior art's defect, provide a sewage purification device, can realize the deep purification at water source, the water after the purification can reach the drinking water standard, can solve global water crisis and general water pollution, improves the fresh water resource capacity on earth's surface.
The utility model discloses a realize like this:
the utility model provides a sewage purification device, which comprises an ultrasonic atomizer, a water molecule adsorber, a high-speed centrifugal desorption device, a centrifugal water collecting cylinder, an ozone generator and a water purification tank;
the inlet end of the ultrasonic atomizer is connected with a sewage source, the outlet end of the ultrasonic atomizer is connected to the water molecule adsorber through a pipeline, and the water molecule adsorber is arranged on the periphery of the high-speed centrifugal desorption device and is driven to rotate by the high-speed centrifugal desorption device;
the centrifugal water collecting cylinder is arranged on the periphery of the water molecule adsorber and is connected with the purified water tank; the ozone generator is connected with the water molecule adsorber through a pipeline.
Furthermore, the outlet end of the ultrasonic atomizer is connected with the water molecule adsorber through an air duct, and the ozone generator is connected with the water molecule adsorber through a tetrafluoride tube.
Further, the water molecule adsorber comprises an adsorption material, and the adsorption material is an SWS composite adsorption material formed by silica gel and CaCl 2.
Further, the water molecule adsorber, the high-speed centrifugal desorption device and the centrifugal water collecting barrel are coaxially arranged.
Furthermore, the inner side of the centrifugal water collecting cylinder is provided with a water guide groove corresponding to the water molecule adsorber, and the water guide groove is connected with the purified water tank.
The utility model discloses following beneficial effect has:
according to the technical scheme of the utility model, sewage is sent into the ultrasonic atomizer for atomization treatment, heavy metal and impurities are precipitated, humid air generated by atomization is sucked into an adsorption material by the water molecule adsorber through the input water molecule adsorber under the strong adsorption effect of the water molecule adsorber, and the adsorption material is filled with water; the high-speed centrifugal desorption device is used for desorbing moisture in the adsorption material and enabling the water to flow into the purified water tank through the centrifugal water collecting cylinder; meanwhile, the ozone generator sends ozone gas into the water molecule absorber to deeply purify the water source in the water molecule absorber, thereby realizing sterilization, sewage removal and oxygen increase. The utility model provides a sewage purification device can realize the deep purification at water source, and the water after the purification can reach the drinking water standard, can solve global water crisis and general water pollution, improves the fresh water resource capacity of earth's surface.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without inventive exercise.
Fig. 1 is a schematic structural diagram of a sewage purification device provided by the embodiment of the utility model.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
The embodiment of the utility model provides a sewage purification method, including following step:
the method comprises the following steps: carrying out atomization treatment on the sewage to precipitate heavy metals and impurities contained in the sewage, wherein water molecules after atomization form humid air; further, the sewage is atomized by ultrasonic waves to atomize the sewage molecular groups containing heavy metals, inorganic substances and organic substances into single water molecules (diameter 4 × 10)^-10m, mass 2.99X 10^-26kg, volume 3X 10^-29m3) Its mass is far less than most heavy metals, pollutants, etc. The water molecules are activated to rise, heavy metals and impurities are naturally precipitated, the separation of the water molecules and pollutants is realized, and the purpose of sewage purification is achieved.
In the first step, effective atomization of water molecule groups is realized by selecting ultrasonic frequency, and single water molecule is formed. The single molecule is driven by heat to naturally rise to form humid air which contains a large amount of water molecules. Specifically, the atomization of water is generated by using an ultrasonic generator, and the water is activated by an ultrasonic sheet which moves back and forth to form atomized water droplets. The higher the ultrasonic frequency, the smaller the diameter of the water droplets produced. When the ultrasonic frequency reaches a certain frequency, the water is completely activated and is suspended in the air in the form of water molecules; the water molecules meet the cold surface of the evaporator and are condensed into water. The frequency of the ultrasonic waves can be selected according to the actual sewage condition, and the requirement can be met as long as the effective atomization of water molecule groups can be realized to form a single water molecule; of course, the higher the frequency of the ultrasonic wave, the better the atomization effect.
Step two: and (3) carrying out ozone sterilization treatment on the humid air formed in the step, and simultaneously carrying out adsorption treatment through an adsorption material.
In the second step, a material with strong adsorption efficiency is used to absorb, collect and desorb water molecules in the air to form a clean water source. Meanwhile, ozone gas with a certain concentration is injected in the adsorption process and reacts with water molecules to achieve the effects of sterilization, sewage removal and oxygen increase, a clean water source is obtained, and sewage purification is realized. The selection of the adsorbent material is specifically: different adsorbent materials have different water adsorption capacities. Parameters of the high-efficiency adsorbing material: the ratio of the mass of adsorbed water to the mass of the adsorbent material itself is referred to as the "mass fraction adsorbed". The adsorption material adopted in the technical scheme is a compound SWS formed by silica gel and CaCl2, and the maximum adsorption mass fraction is about 90%; the maximum adsorption mass fraction of the common molecular sieve is only 25%, the adsorption mass fraction of the common silica gel is about 40%, and the water production efficiency is greatly improved by using the high-efficiency adsorption material.
Step three: and (4) dehydrating the adsorption material subjected to adsorption treatment, so that the purification of sewage can be realized. In the step, the high-speed centrifugal equipment is used for dehydrating the adsorption material, so that the purified water is separated from the adsorption material, and the water resource is purified and stored.
As shown in FIG. 1, the utility model also provides a sewage purification device, the working principle of which is the whole process of the above sewage purification method. The sewage purification device comprises an ultrasonic atomizer 1, a water molecule absorber 2, a high-speed centrifugal desorption device 3, a centrifugal water collecting cylinder 4, an ozone generator 5 and a water purification tank 6;
as shown in fig. 1, the inlet end of the ultrasonic atomizer 1 is connected to a sewage source, and is used for atomizing the sewage in one of the above steps, so that heavy metals and impurities contained in the sewage are precipitated, and the atomized water molecules form humid air.
As shown in fig. 1, the outlet end of the ultrasonic atomizer 1 is connected to the water molecule adsorber 2 through a pipeline, and is used for introducing atomized water molecules into the water molecule adsorber 2; the water molecule adsorber 2 comprises an adsorption material, and the adsorption material is an SWS composite adsorption material formed by silica gel and CaCl 2. The water molecule adsorber 2 can effectively adsorb the atomized humid air. Furthermore, the outlet end of the ultrasonic atomizer 1 is connected with the water molecule adsorber 2 through an air duct, and the air duct is used for guiding humid air and has basic functions of corrosion resistance, aging resistance and the like.
As shown in fig. 1, the water molecule adsorber 2 is disposed on the outer periphery of the high-speed centrifugal separator 3, and is driven to rotate by the high-speed centrifugal separator 3; the high-speed centrifugal desorption device 3 runs through a motor so as to drive the water molecule adsorber 2 to rotate centrifugally, and when the centrifugal force exceeds the binding force of the water and the adsorption material, the water in the adsorption material can be thrown out towards the outer side.
As shown in fig. 1, the centrifugal water collecting cylinder 4 is disposed on the outer periphery of the water molecule adsorber 2; the centrifugal water collecting cylinder 4 is connected with the purified water tank 6. The centrifugal water collecting cylinder 4 is used for receiving the water separated from the adsorption material of the water molecule adsorber 2 and transmitting the water to the purified water tank 6 for storage. Furthermore, the inner side of the centrifugal water collecting cylinder 4 is provided with a water guide groove corresponding to the water molecule adsorber 2, the water guide groove is connected with the purified water tank 6, and the water guide groove is used for completely guiding water separated from the adsorption material to the purified water tank 6, so that the smoothness of the whole water circulation is ensured. Wherein, the centrifugal water collecting cylinder 4 is sleeved outside the water molecule adsorber 2, and is convenient to install and disassemble.
As shown in fig. 1, in the preferred embodiment, the water molecule adsorber 2, the high-speed centrifugal separator 3 and the centrifugal water collecting cylinder 4 are coaxially arranged, so that the centrifugal operation of the high-speed centrifugal separator 3 can be effectively ensured, and the water absorbed by the water molecule adsorber 2 can be substantially separated.
As shown in fig. 1, the ozone generator 5 is connected to the water molecule adsorber 2 through a pipe. Further, the ozone generator 5 is connected to the water molecule adsorber 2 through a tetrafluoro pipe. The ozone generator 5 is used for generating ozone, the ozone is transmitted into the water molecule adsorber 2 through the tetrafluoride pipe, and the humid air (water vapor) inside the ozone generator is purified and sterilized, so that the effects of sterilization, decontamination and oxygen increase are achieved, and a clean water source is obtained.
The operation of the ultrasonic atomizer 1 and the high-speed centrifugal desorption device 3 can be controlled by people, the ultrasonic atomizer and the high-speed centrifugal desorption device 3 are correspondingly provided with switches, the high-speed centrifugal desorption device 3 is driven by a motor to operate, the adsorption material of the water molecule adsorber 2 is arranged on the periphery of the high-speed centrifugal desorption device 3, and the dehydration operation can be carried out under the action of centrifugal force; the centrifugal water collecting cylinder 4 is fixed and used for receiving water and guiding the water to the purified water tank 6. The control of the ozone generator 5 is also performed on an artificial basis. The selection of the actual ozone concentration can be treated as follows: the ozone concentration refers to the content of ozone in the air or water. The concentration in water is in PPM, which represents the mass of solute contained in one million parts per mass of solution, and is called several PPM in PPM, which is (mass of solute/mass of solution) × 1000000. When ozone is used for purifying water, the concentration is too low to achieve the effect of sterilization and decontamination, the concentration is too high to cause the price of deodorization and oxygen to be too high, and more adsorbing materials are used for eliminating the ozone in the water to achieve the standard of drinking water; the national standard for the ozone content in water is not higher than 0.05 PPM.
To sum up, the technical scheme of the utility model is that sewage is sent into the ultrasonic atomizer 1 for atomization treatment, heavy metal and impurities are precipitated, the humid air generated by atomization is absorbed into the adsorption material of the water molecule absorber 2 through the input water molecule absorber 2 under the strong adsorption effect of the water molecule absorber, and the adsorption material is full of water; the high-speed centrifugal desorption device 3 is used for desorbing moisture in the adsorption material and flowing into the purified water tank 6 through the centrifugal water collecting cylinder 4; meanwhile, the ozone generator 5 sends ozone gas into the water molecule absorber 2 to deeply purify the water source in the water molecule absorber, thereby realizing sterilization, sewage removal and oxygen increase. The utility model provides a sewage purification device and sewage purification method can realize the deep purification at water source, and the water after the purification can reach the drinking water standard, can solve global water crisis and universal water pollution, improves the fresh water resource capacity on earth's surface.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (4)
1. A sewage purification device is characterized by comprising an ultrasonic atomizer, a water molecule adsorber, a high-speed centrifugal desorption device, a centrifugal water collecting cylinder, an ozone generator and a water purification tank;
the inlet end of the ultrasonic atomizer is connected with a sewage source, the outlet end of the ultrasonic atomizer is connected to the water molecule adsorber through a pipeline, and the water molecule adsorber is arranged on the periphery of the high-speed centrifugal desorption device and is driven to rotate by the high-speed centrifugal desorption device;
the centrifugal water collecting cylinder is arranged on the periphery of the water molecule adsorber and is connected with the purified water tank; the ozone generator is connected with the water molecule adsorber through a pipeline.
2. The sewage purification apparatus according to claim 1, wherein: the outlet end of the ultrasonic atomizer is connected with the water molecule adsorber through an air duct, and the ozone generator is connected with the water molecule adsorber through a tetrafluoride tube.
3. The sewage purification apparatus according to claim 1, wherein: the water molecule adsorber, the high-speed centrifugal desorption device and the centrifugal water collecting barrel are coaxially arranged.
4. The sewage purification apparatus according to claim 1, wherein: the inner side of the centrifugal water collecting cylinder is provided with a water guide groove corresponding to the water molecule adsorber, and the water guide groove is connected with the purified water tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920511085.8U CN210711094U (en) | 2019-04-16 | 2019-04-16 | Sewage purification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920511085.8U CN210711094U (en) | 2019-04-16 | 2019-04-16 | Sewage purification device |
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| Publication Number | Publication Date |
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| CN210711094U true CN210711094U (en) | 2020-06-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920511085.8U Expired - Fee Related CN210711094U (en) | 2019-04-16 | 2019-04-16 | Sewage purification device |
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| CN (1) | CN210711094U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109851120A (en) * | 2019-04-16 | 2019-06-07 | 梁毅强 | A kind of effluent treatment plant and effluent purification method |
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2019
- 2019-04-16 CN CN201920511085.8U patent/CN210711094U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109851120A (en) * | 2019-04-16 | 2019-06-07 | 梁毅强 | A kind of effluent treatment plant and effluent purification method |
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Granted publication date: 20200609 |