CN109534527A - A kind of low-purity oxygen plant accelerating black and odorous water ecosystem restoration - Google Patents
A kind of low-purity oxygen plant accelerating black and odorous water ecosystem restoration Download PDFInfo
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- CN109534527A CN109534527A CN201910082064.3A CN201910082064A CN109534527A CN 109534527 A CN109534527 A CN 109534527A CN 201910082064 A CN201910082064 A CN 201910082064A CN 109534527 A CN109534527 A CN 109534527A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 165
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 239000001301 oxygen Substances 0.000 title claims abstract description 30
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 30
- 238000002156 mixing Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 230000008676 import Effects 0.000 claims abstract description 14
- 230000001105 regulatory effect Effects 0.000 claims description 16
- 230000007704 transition Effects 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 16
- 238000005516 engineering process Methods 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 12
- 239000007789 gas Substances 0.000 description 19
- 102000010637 Aquaporins Human genes 0.000 description 16
- 108091006146 Channels Proteins 0.000 description 12
- 239000002101 nanobubble Substances 0.000 description 12
- 238000005273 aeration Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000004090 dissolution Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 4
- -1 hydroxyl radical free radical Chemical class 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 230000001154 acute effect Effects 0.000 description 2
- 230000008034 disappearance Effects 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 102000012002 Aquaporin 4 Human genes 0.000 description 1
- 108010036280 Aquaporin 4 Proteins 0.000 description 1
- 108010063290 Aquaporins Proteins 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/03—Pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/22—O2
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
Abstract
The invention discloses a kind of low-purity oxygen plants for accelerating black and odorous water ecosystem restoration, comprising: has water inlet, air inlet and the water inlet air pipe of third water mouth out；The third water mouth that goes out of gas-liquid mixing pump, air pipe of intaking is connected with the import of gas-liquid mixing pump；With water inlet port and the dissolving of dissolved air water mouth out, port of intaking is connected with the outlet of gas-liquid mixing pump；Dissolved air water pipeline out, import are connected with the dissolved air water mouth that goes out of dissolving；And micro bubble releasing device, it is mounted on out the outlet of dissolved air water pipeline.The low-purity oxygen plant goes out microbubble technology and bleed manufacture bubbler techniques manufacture microbubble in conjunction with molten air elutriation, solve the problems, such as manufacturing process and operation it is all more troublesome, to bubble generator requirement is high, manufactured Air Bubble Size is uneven, cost is high.
Description
Technical field
Present document relates to technical field of environmental equipment, espespecially a kind of low-purity oxygen plant for accelerating black and odorous water ecosystem restoration.
Background technique
Along with the quick process of industrialization and urbanization, a large amount of waste water and contaminated rainwash have little time to collect
It is directly discharged into river with processing, along with the untreated discharge of agricultural effluent, the amount of being included in of Mixing Coefficient in Rectangular Channels has been more than purification energy
Black smelly phenomenon is presented in power, river.The main governing measure of black and odorous water has physical method, chemical method and biological and ecological method and group
Conjunction method.River aeration technology is preferentially adopted as a kind of small investment, quick Discussion On Measures of Rivers Pollution Treatment technology in many countries
With.River aeration technology is manually to be filled with air (or oxygen) into water body the characteristics of being contaminated rear anoxic according to river, add
Fast water reoxygenation process is restored and is enhanced the vigor of aerobic microbiological in water body to improve the oxygen level of melting of water body, make water body
In polluter be purified, so as to improve the water quality in river.
River aeration technology mainly has following three classes method:
One, molten air elutriation goes out microbubble technology, and the bubble size of manufacture is small, uniform in size, and size is on 10~100 μm of left sides
The right side, advantage is that microbubble can stop in water for a long time, the disadvantage is that manufacturing process and operation are all more troublesome；
Two, bleed manufactures microbubble technology, manufactures bubble diameter between 0.5~1.0mm, and molten large-minded, low energy consumption,
Separation equipment is simple, but requires height to bubble generator, and Air Bubble Size is uneven；
Three, microbubble technology is precipitated in electrolysis, generates in such a way that electrolytic cell positive/negative plate generates bubble hydrogen and oxygen bubbles
Microbubble of the diameter between 20~60 μm, the bubble size that this method generates is small, but polar plate loss is big, cost also very
It is high.
Summary of the invention
At least one of in order to solve the above-mentioned technical problem, there is provided herein a kind of acceleration black and odorous water ecosystem is extensive
Multiple low-purity oxygen plant goes out microbubble technology and bleed manufacture bubbler techniques manufacture microbubble in conjunction with molten air elutriation, solves manufacture stream
Journey and operation are all more troublesome, require bubble generator the problem high, manufactured Air Bubble Size is uneven, cost is high.
Low-purity oxygen plant provided in an embodiment of the present invention, comprising: there is water inlet, air inlet and the water inlet tracheae of third water mouth out
Road；The third water mouth that goes out of gas-liquid mixing pump, the water inlet air pipe is connected with the import of the gas-liquid mixing pump；With influent gas
The dissolving of mouth and out dissolved air water mouth, water inlet port are connected with the outlet of the gas-liquid mixing pump；Dissolved air water pipeline out,
Import is connected with the dissolved air water mouth that goes out of the dissolving；And micro bubble releasing device, it is mounted on going out for the dissolved air water pipeline out
Mouthful.
Optionally, the micro bubble releasing device is micron-sized micro bubble releasing device.
Optionally, the water inlet air pipe includes: inlet pipeline, and import is the water inlet；With jet stream air inlet pipe,
It is that third water mouth, the air inlet out are located at the jet stream air inlet that import, which is connected with the outlet of the inlet pipeline, exports,
Guan Shang is simultaneously between the inlet and outlet of the jet stream air inlet pipe.
Optionally, the jet stream air inlet pipe includes the intake tunnel being sequentially communicated, mixing chamber and aqueous vapor channel out, it is described into
The internal diameter of aquaporin and the internal diameter in the aqueous vapor channel out are respectively less than the internal diameter of the mixing chamber, and the air inlet is located at described mixed
It closes on chamber.
Optionally, the mixing chamber includes abruptly increase section and converging transition, and the intake tunnel is connected to the abruptly increase section, described
Aqueous vapor channel is connected to the converging transition out, and the air inlet is located in the abruptly increase section, and the internal diameter of the intake tunnel is tapered.
Optionally, the internal diameter of the intake tunnel rear end is greater than 6~10mm of internal diameter of front end, and the internal diameter of the abruptly increase section is big
4~8mm of internal diameter in the intake tunnel rear end, the internal diameter of the intake tunnel rear end are greater than the internal diameter in the aqueous vapor channel out
4~8mm.
Optionally, the micro bubble releasing device includes: into dissolved air water pipeline section；Conducting element is arranged described into dissolved air water pipe
In section, the conducting element and described into being formed between dissolved air water pipeline section into dissolved air water channel, the side of the conducting element is gradually wealthy
Guide face, the conducting element front end face recess have extension slot；Turbulent chamber, positioned at the conducting element front side and with it is described
It is connected into dissolved air water channel, the anterior cavity wall of the turbulent flow chamber forms baffling portion, and the extension slot is connected to the turbulent chamber；With go out
Microbubble water channel is arranged on the anterior cavity wall of the turbulent chamber.
Optionally, the guide face is tapered surface, and the extension slot is cone tank, the internal diameter in the microbubble water channel out
It is gradually wealthy.
Optionally, the front end face of the conducting element and the radial distance between dissolved air water pipeline section are 6~10mm, institute
The axial distance stated between the front end face of conducting element and the anterior cavity wall of the turbulent chamber is 2~4mm, the microbubble water channel out
The internal diameter of rear end is 2~4mm, and the width of the outer end face of the cone tank is 0.5~2.5mm, and the cone angle of the cone tank is 80
~100 degree, the cone angle of the tapered surface is 10~30 degree.
Optionally, regulating valve is installed on the air inlet, pressure sensor, the pressure are provided on the dissolving
Sensor is connected with the regulating valve, and the top of the dissolving is provided with exhaust outlet, and exhaust is provided on the exhaust outlet
The water inlet of valve, the water inlet air pipe is provided with strainer valve.
Optionally, the regulating valve is automatic regulating valve, and the exhaust valve is automatic exhaust steam valve.
Compared with prior art, low-purity oxygen plant provided by the invention goes out microbubble technology in conjunction with molten air elutriation and bleed manufactures
Bubbler techniques are intake, air inlet by water inlet air pipe before entering gas-liquid mixing pump, are sufficiently mixed air water in equipment
Dissolution forms dissolved air water, microbubble most is precipitated through micro bubble releasing device afterwards, the device structure is simple, equipment requirement is low, solves
Manufacturing process and operation are all more troublesome, require bubble generator height, manufactured Air Bubble Size is uneven, cost is high
Problem, the practicality is more preferable, and the microbubble of precipitation can effectively administer black and odorous water, purify water in river aeration.
The low-purity oxygen plant, the bubble diameter being precipitated can be stablized at 50 μm or so, and the microbubble of precipitation has following excellent
Point:
1, the residence time is long in water: it is compared with Centimeter Level bubble, it, can be quick after Centimeter Level bubble generates in water body
Rise to the water surface and rupture disappearance, the residence time in water body is too short, and dissolved oxygen effect is poor, and micro-nano bubble in water on
The speed risen is slower, and the time from generating rupture can achieve tens seconds or even a few minutes.
2, itself pressurization dissolution: there are the contact interface of gas-liquid two-phase, the presence of gas-liquid interface makes the bubble surface in water
Surface tension effects of the bubble by water are obtained, surface tension effects can compress the gas in bubble, so that gas is easier to
It is dissolved into water, the surface tension that micro-nano bubble is subject to is much larger than Centimeter Level bubble, it can be gradually reduced, final completely molten
Solution.
3, interface zeta potential is high: when micro-nano bubble is shunk in water, electrically charged ion is able to carry out on bubble interface
Enrichment method, shows as dramatically increasing for zeta potential, can produce very high zeta potential value, zeta potential value before bubbles burst
It is an important factor for influencing bubble surface absorption property, the size of value can generate the absorption property of micro-nano bubble interface
Significantly influence.
4, generate hydroxyl radical free radical: micro-nano bubble is when shrinking, since the charge density of electric double layer increases rapidly, bubble
When rupture, the acute variation that gas-liquid interface disappears discharges the energy of the negative ions savings of high concentration on interface, can swash at this time
Hair generates a large amount of hydroxyl radical free radical.
These advantages of micro-nano bubble, make it in river aeration, can effectively administer black and odorous water, purify water.
The other feature and advantage of this paper will illustrate in the following description, also, partly become from specification
It is clear that by implementing to understand herein.The purpose of this paper and other advantages can be by specifications, claims
And specifically noted structure is achieved and obtained in attached drawing.
Detailed description of the invention
Attached drawing is used to provide to further understand this paper technical solution, and constitutes part of specification, with this Shen
Embodiment please is used to explain the technical solution of this paper together, does not constitute the limitation to this paper technical solution.
Fig. 1 is the schematic perspective view of low-purity oxygen plant described in one embodiment of the invention；
Fig. 2 is the front view structure diagrammatic cross-section of jet stream air inlet pipe in Fig. 1；
Fig. 3 is the front view structure diagrammatic cross-section of jet stream air inlet pipe in Fig. 1；
Fig. 4 is the left view schematic structural cross-sectional view of jet stream air inlet pipe shown in Fig. 3.
Wherein, the corresponding relationship in Fig. 1 to Fig. 4 between appended drawing reference and component names are as follows:
1 gas-liquid mixing pump, 2 dissolvings, 21 automatic exhaust steam valves, 22 exhaust nozzles, 3 go out dissolved air water pipeline, the release of 4 microbubbles
Device, 41 into dissolved air water pipeline section, and 42 conducting elements, 43 into dissolved air water channel, and 44 extension slots, 45 turbulent chambers, 46 baffling portions, 47 go out micro- gas
Soaked channel, 48 brackets, 51 inlet pipelines, 52 jet stream air inlet pipe, 521 intake tunnels, 522 mixing chambers, 523 go out aqueous vapor channel,
524 air inlets, 53 automatic regulating valves, 54 suction nozzles, 55 pressure sensors, 56 strainer valves, 6 shells, 61 display screens.
Specific embodiment
For the purposes, technical schemes and advantages of this paper are more clearly understood, below in conjunction with attached drawing to the reality of this paper
Example is applied to be described in detail.It should be noted that in the absence of conflict, the spy in embodiment and embodiment in the application
Sign can mutual any combination.
Many details are explained in the following description in order to fully understand herein, still, can also be adopted herein
Implemented with other than the one described here mode, therefore, the protection scope of this paper is not by following public specific implementation
The limitation of example.
Low-purity oxygen plant provided in an embodiment of the present invention, as shown in Figure 1, comprising: there is water inlet, air inlet and third water mouth out
Water inlet air pipe；The third water mouth that goes out of gas-liquid mixing pump 1, air pipe of intaking is connected with the import of gas-liquid mixing pump 1；With into
The dissolving 2 of third water mouth and out dissolved air water mouth, water inlet port are connected with the outlet of gas-liquid mixing pump 1；Dissolved air water pipeline out
3, import is connected with the dissolved air water mouth that goes out of dissolving 2；With micron-sized micro bubble releasing device 4, it is mounted on out dissolved air water pipe
The outlet on road 3.
The low-purity oxygen plant goes out microbubble technology in conjunction with molten air elutriation and bleed manufactures bubbler techniques, is entering gas-liquid mixing pump 1
It is intake before by water inlet air pipe, air inlet, air water is made to be sufficiently mixed dissolution in equipment, dissolved air water is formed, most afterwards through micro-
Microbubble is precipitated in bubble release 4, and the device structure is simple, equipment requirement is low, solves manufacturing process and operation is all number
Tired, high to bubble generator requirement, manufactured Air Bubble Size is uneven, cost is high problem, the practicality is more preferable, is precipitated
Microbubble in river aeration, can effectively administer black and odorous water, purify water.Arrow indicates aqueous vapor transmission direction in Fig. 1.
Specifically: it is intake before entering gas-liquid mixing pump 1 by water inlet air pipe, air inlet, due to gas-liquid mixing pump 1
Pump case in be in high voltage state, portion of air is soluble in water in the pump case of gas-liquid mixing pump 1, and in gas-liquid mixing pump 1
Impeller smashes undissolved air, stirs into water, and the water outlet of gas-liquid mixing pump 1 at this time includes dissolved air water and remaining undissolved air,
And be pumped into dissolving 2, since 2 volume of dissolving is big, so that also increasing therewith into the air of dissolving 2 and the contact area of water
Greatly, after remaining undissolved air and dissolved air water come into full contact with, partial air is dissolved in the water to form saturated dissolved gas water, saturated dissolved gas
Water flows through micro bubble releasing device 4, and gas dissolved water is released with micron level bubble, forms milky microbubble water.
Wherein, as shown in Figure 1, water inlet air pipe includes: inlet pipeline 51, import is water inlet；With jet stream air inlet pipe
52, import is connected with the outlet of inlet pipeline 51, exports to go out third water mouth, and air inlet is located in jet stream air inlet pipe 52, simultaneously
Between inlet and outlet in jet stream air inlet pipe 52.Moreover, regulating valve can be equipped on air inlet, regulating valve be connected with into
Pressure sensor 55 has can be set on dissolving 2 in gas nozzle 54, and pressure sensor 55 is connected with regulating valve, dissolving 2 it is upper
Portion is provided with exhaust outlet, and exhaust valve 21 is provided on exhaust outlet, and exhaust valve 21 connects exhaust nozzle 22, the water inlet of inlet pipeline 51
It is provided with strainer valve 56.Regulating valve is preferably configured to automatic regulating valve 53, and exhaust valve 21 is preferably configured to automatic exhaust steam valve 21.Benefit
Pressure in dissolving 2 is acquired with pressure sensor 55, then automatic regulating valve 53 voluntarily adjusts according to pressure change, automatically controls
Air inflow does not need to manually adjust air inflow, and operation is more stable, avoids causing 2 pressure of dissolving to decline because air inflow increases,
So that the problem of gas-liquid mixing pump 1 dallies.
Low-purity oxygen plant further includes the shell 6 such as stainless steel material, is provided with human-computer interaction device, human-computer interaction on shell 6
Device includes display screen 61, for controlling equipment start-stop, the pressure for showing pressure sensor 55 etc..
Under working condition, gas-liquid mixing pump 1 is aspirated, and water is filtered to remove large granular impurity by strainer valve 56, by jet stream
When air inlet pipe 52, flow velocity is accelerated.Air reaches in jet stream air inlet pipe 52 by suction nozzle 54 along automatic regulating valve 53, passes through with water
One preliminary mixing, into gas-liquid mixing pump 1, due to being in high voltage state in the pump case of gas-liquid mixing pump 1, portion of air is in gas
It is soluble in water in the pump case of liquid mixing pump 1, and the impeller in gas-liquid mixing pump 1 smashes undissolved air, stirs into water, this
When the water outlet of gas-liquid mixing pump 1 include dissolved air water and remaining undissolved air, and be pumped into dissolving 2, due to 2 volume of dissolving
Greatly, so that also increasing with it into the air of dissolving 2 and the contact area of water, remaining undissolved air sufficiently connects with dissolved air water
After touch, portion of air is dissolved in the water to form saturated dissolved gas water, and the undissolved air of another part is by automatic exhaust steam valve 21 through arranging
Gas nozzle 22 is discharged, and avoids undissolved air capacity persistent accumulation in dissolving 2 and occupies the volume in dissolving 2.Saturated dissolved gas water
Micro bubble releasing device 4 is flowed through, gas dissolved water is released with micron level bubble, forms milky microbubble water.Entirely
Manufacture microbubble process, pressure in 55 real-time monitoring dissolving 2 of pressure sensor, the dissolving detected according to pressure sensor 55
Pressure automatic regulating valve 53 opens and closes amplitude in 2, and then automatically adjusts air inflow.
In one exemplary embodiment, as shown in Fig. 2, jet stream air inlet pipe 52 includes the intake tunnel 521 being sequentially communicated, mixes
Close chamber 522 and aqueous vapor channel 523 out, the internal diameter of the intake tunnel 521 and internal diameter in aqueous vapor channel 523 is respectively less than mixing chamber 522 out
Internal diameter, air inlet is located on mixing chamber 522.Mixing chamber 522 includes that the converging transition of cylindrical abruptly increase section and cone is (tapered
Angle can be set to 150 degree), intake tunnel 521 is connected to abruptly increase section, and aqueous vapor channel 523 is connected to converging transition out, air inlet
524 are located in abruptly increase section, and the internal diameter of intake tunnel 521 is tapered (taper angle can be set to 30 degree).
The water being inhaled into enters jet stream air inlet pipe 52 from intake tunnel 521, after the inner diameter wall of 521 front end of intake tunnel
End it is small, flow rate of water flow is accelerated, and quick water flow enters mixing chamber 522, negative pressure can be formed in mixing chamber 522, thus air pass through into
Port is inhaled into mixing chamber 522, while the converging transition of mixing chamber 522 reduces along water (flow) direction area of section, gas can be made along water
Stream direction is compressed, and will form a preliminary mixing with water, most enters gas-liquid mixing pump 1 through water outlet gas channel 523 afterwards.
Specifically, the internal diameter of 521 rear end of intake tunnel is set greater than 6~10mm of internal diameter (such as 8mm) of front end, abruptly increase section
Internal diameter be set greater than 4~8mm of internal diameter (such as 6mm) of 521 rear end of intake tunnel, the internal diameter setting of 521 rear end of intake tunnel
For 4~8mm of internal diameter (such as 6mm) greater than aqueous vapor channel 523 out.
In one exemplary embodiment, as shown in Figure 3 and Figure 4, micro bubble releasing device 4 includes: into dissolved air water pipeline section 41；It leads
Flow part 42, setting is into dissolved air water pipeline section 41, conducting element 42 and into being formed between dissolved air water pipeline section 41 into dissolved air water channel 43,
The side of conducting element 42 is gradually wealthy guide face, and the front end face recess of conducting element 42 has extension slot 44；Turbulent chamber 45 is located at water conservancy diversion
The front side of part 42 is simultaneously connected into dissolved air water channel 43, and the anterior cavity wall of turbulent chamber 45 forms baffling portion 46, extension slot 44 and turbulent flow
Chamber 45 is connected to；Microbubble water channel 47 out is arranged on the anterior cavity wall of turbulent chamber 45.Guide face is set as tapered surface, extends
Slot 44 is set as cone tank, and the internal diameter in microbubble water channel 47 is gradually wealthy out.Conducting element 42 can be mounted on by bracket 48 into molten
In air water pipeline section 41.
Water flow is by entering micro bubble releasing device 4 into dissolved air water pipeline section 41, through guide face by water flow along into dissolved air water channel 43
Transmission reaches turbulent chamber 45, impacts in baffling portion 46, water flow is directed in cone tank, and in cone tank, water flow mutually bumps against
It hits, turbulent flow aggravation, part dissolved gas is released in the form of microbubble in water flow, and then water flow enters microbubble water channel
47, the area of section due to going out 47 rear end of microbubble water channel acutely reduces relative to turbulent chamber 45, and water flow is greatly accelerated, is pressed
It can reduce, dissolved gas is released completely in the form of microbubble, is transmitted when passing through microbubble water channel 47 with bladdery water
When, the area of section due to going out microbubble water channel 47 is gradually increased, and with bladdery water flow, speed is reduced, and pressure energy increases, water
Middle bubble is compressed, and bubble diameter further reduces, and the bubble of precipitation is micron order.
Specifically, the front end face of conducting element 42 and into the radial distance between dissolved air water pipeline section 41 be 6~10mm (such as
8mm), the axial distance between the front end face of conducting element 42 and the anterior cavity wall of turbulent chamber 45 is 2~4mm (such as 3mm), out microbubble
The internal diameter of 7 rear end of aquaporin-4 is 2~4mm (such as 3mm), and the width of the outer end face of cone tank is 0.5~2.5mm (such as 1.5mm),
The cone angle of cone tank is 80~100 degree (such as 90 degree), and the cone angle of tapered surface is 10~30 degree (such as 20 degree).
The low-purity oxygen plant, the bubble diameter being precipitated can be stablized at 50 μm or so, have the advantages that
1, the residence time is long in water: it is compared with Centimeter Level bubble, it, can be quick after Centimeter Level bubble generates in water body
Rise to the water surface and rupture disappearance, the residence time in water body is too short, and dissolved oxygen effect is poor, and micro-nano bubble in water on
The speed risen is slower, and the time from generating rupture can achieve tens seconds or even a few minutes.
2, itself pressurization dissolution: there are the contact interface of gas-liquid two-phase, the presence of gas-liquid interface makes the bubble surface in water
Surface tension effects of the bubble by water are obtained, surface tension effects can compress the gas in bubble, so that gas is easier to
It is dissolved into water, the surface tension that micro-nano bubble is subject to is much larger than Centimeter Level bubble, it can be gradually reduced, final completely molten
Solution.
3, interface zeta potential is high: when micro-nano bubble is shunk in water, electrically charged ion is able to carry out on bubble interface
Enrichment method, shows as dramatically increasing for zeta potential, can produce very high zeta potential value, zeta potential value before bubbles burst
It is an important factor for influencing bubble surface absorption property, the size of value can generate the absorption property of micro-nano bubble interface
Significantly influence.
4, generate hydroxyl radical free radical: micro-nano bubble is when shrinking, since the charge density of electric double layer increases rapidly, bubble
When rupture, the acute variation that gas-liquid interface disappears discharges the energy of the negative ions savings of high concentration on interface, can swash at this time
Hair generates a large amount of hydroxyl radical free radical.
These advantages of micro-nano bubble, make it in river aeration, can effectively administer black and odorous water, purify water.
Arrow indicates aqueous vapor transmission direction in Fig. 1, and "front", "rear", " tapered " in the application, " gradually wealthy " are along water flow
The restriction that transmission direction carries out.
In conclusion low-purity oxygen plant provided by the invention, goes out microbubble technology in conjunction with molten air elutriation and bleed manufactures bubble skill
Art is intake, air inlet by water inlet air pipe before entering gas-liquid mixing pump, air water is made to be sufficiently mixed dissolution in equipment,
Dissolved air water is formed, microbubble most is precipitated through micro bubble releasing device afterwards, the device structure is simple, equipment requirement is low, solves manufacture
Process and operation are all more troublesome, require high, manufactured Air Bubble Size is uneven, cost is high to ask bubble generator
Topic, the practicality is more preferable, and the microbubble of precipitation can effectively administer black and odorous water, purify water in river aeration.
In description herein, term " installation ", " connected ", " connection ", " fixation " etc. be shall be understood in a broad sense, for example,
" connection " may be fixed connection or may be dismantle connection, or integral connection；It can be directly connected, can also lead to
Intermediary is crossed to be indirectly connected.For the ordinary skill in the art, above-mentioned term can be understood as the case may be
Concrete meaning herein.
In the description of this specification, the description of term " one embodiment ", " some embodiments ", " specific embodiment " etc.
Mean that particular features, structures, materials, or characteristics described in conjunction with this embodiment or example are contained at least one implementation of this paper
In example or example.In the present specification, schematic expression of the above terms are not necessarily referring to identical embodiment or example.
Moreover, the particular features, structures, materials, or characteristics of description can be in any one or more of the embodiments or examples with suitable
Mode combine.
Although embodiment disclosed herein is as above, the content only implementation of use herein for ease of understanding
Mode is not limited to herein.Technical staff in any this paper fields, do not depart from spirit disclosed herein and
Under the premise of range, any modification and variation, but the patent protection model of this paper can be carried out in the form and details of implementation
It encloses, still should be subject to the scope of the claims as defined in the appended claims.
Claims (10)
1. a kind of low-purity oxygen plant characterized by comprising
With water inlet, air inlet and the water inlet air pipe of third water mouth out；
The third water mouth that goes out of gas-liquid mixing pump, the water inlet air pipe is connected with the import of the gas-liquid mixing pump；
With water inlet port and the dissolving of dissolved air water mouth out, port of intaking is connected with the outlet of the gas-liquid mixing pump；
Dissolved air water pipeline out, import are connected with the dissolved air water mouth that goes out of the dissolving；With
Micro bubble releasing device is mounted on the outlet of the dissolved air water pipeline out.
2. low-purity oxygen plant according to claim 1, which is characterized in that the water inlet air pipe includes:
Inlet pipeline, import are the water inlet；With
Jet stream air inlet pipe, import are connected with the outlet of the inlet pipeline, export as the third water mouth out, the air inlet
In the jet stream air inlet pipe and between the inlet and outlet in the jet stream air inlet pipe.
3. low-purity oxygen plant according to claim 2, which is characterized in that the jet stream air inlet pipe includes the water inlet being sequentially communicated
Channel, mixing chamber and aqueous vapor channel out, the internal diameter of the intake tunnel and it is described go out aqueous vapor channel internal diameter be respectively less than it is described mixed
The internal diameter of chamber is closed, the air inlet is located on the mixing chamber.
4. low-purity oxygen plant according to claim 3, which is characterized in that the mixing chamber includes abruptly increase section and converging transition, institute
It states intake tunnel to be connected to the abruptly increase section, the aqueous vapor channel out is connected to the converging transition, and the air inlet is located at described
In abruptly increase section, the internal diameter of the intake tunnel is tapered.
5. low-purity oxygen plant according to claim 4, which is characterized in that the internal diameter of the intake tunnel rear end is greater than front end
6~10mm of internal diameter, the internal diameter of the abruptly increase section are greater than 4~8mm of internal diameter of the intake tunnel rear end, the intake tunnel rear end
Internal diameter be greater than it is described go out aqueous vapor channel 4~8mm of internal diameter.
6. low-purity oxygen plant according to claim 1, which is characterized in that the micro bubble releasing device includes:
Into dissolved air water pipeline section；
Conducting element, setting into dissolved air water pipeline section, the conducting element and described are formed between dissolved air water pipeline section into molten described
Gas-water channel, the side of the conducting element are gradually wealthy guide face, and the front end face recess of the conducting element has extension slot；
Turbulent chamber, positioned at the conducting element front side and be connected to described into dissolved air water channel, it is described turbulent flow chamber anterior cavity wall shape
At baffling portion, the extension slot is connected to the turbulent chamber；With
Microbubble water channel out is arranged on the anterior cavity wall of the turbulent chamber.
7. low-purity oxygen plant according to claim 6, which is characterized in that the guide face is tapered surface, and the extension slot is
The internal diameter of cone tank, the microbubble water channel out is gradually wealthy.
8. low-purity oxygen plant according to claim 7, which is characterized in that the front end face of the conducting element and described into dissolved air water
Radial distance between pipeline section is 6~10mm, the axial direction between the front end face of the conducting element and the anterior cavity wall of the turbulent chamber
Distance is 2~4mm, and the internal diameter of the microbubble water channel rear end out is 2~4mm, and the width of the outer end face of the cone tank is
0.5~2.5mm, the cone angle of the cone tank are 80~100 degree, and the cone angle of the tapered surface is 10~30 degree.
9. low-purity oxygen plant according to any one of claim 1 to 8, which is characterized in that be equipped with tune on the air inlet
Valve is saved, is provided with pressure sensor on the dissolving, the pressure sensor is connected with the regulating valve, the dissolving
Top be provided with exhaust outlet, be provided with exhaust valve on the exhaust outlet, the water inlet of the water inlet air pipe is provided with filtering
Valve, the micro bubble releasing device are micron-sized micro bubble releasing device.
10. low-purity oxygen plant according to claim 9, which is characterized in that the regulating valve is automatic regulating valve, the exhaust
Valve is automatic exhaust steam valve.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201910082064.3A CN109534527A (en) | 2019-01-28 | 2019-01-28 | A kind of low-purity oxygen plant accelerating black and odorous water ecosystem restoration |
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| CN201910082064.3A CN109534527A (en) | 2019-01-28 | 2019-01-28 | A kind of low-purity oxygen plant accelerating black and odorous water ecosystem restoration |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111747546A (en) * | 2020-07-15 | 2020-10-09 | 合肥济坤环保科技有限责任公司 | Intelligent pure oxygen dissolved gas water body reoxygenation technology and equipment |
| CN115108621A (en) * | 2021-03-23 | 2022-09-27 | 中国科学院上海高等研究院 | Preparation device and method of high-oxygen water |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102219315A (en) * | 2011-06-22 | 2011-10-19 | 昆明迪波泵业有限公司 | High-efficiency energy-saving submicron bubble aeration oxygenating device |
| CN204752263U (en) * | 2015-06-19 | 2015-11-11 | 中国石油大学(华东) | Detachable dissolved air releaser |
| CN108946969A (en) * | 2018-06-08 | 2018-12-07 | 广州资源环保科技股份有限公司 | A kind of aeration system based on micro-nano bubble |
-
2019
- 2019-01-28 CN CN201910082064.3A patent/CN109534527A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102219315A (en) * | 2011-06-22 | 2011-10-19 | 昆明迪波泵业有限公司 | High-efficiency energy-saving submicron bubble aeration oxygenating device |
| CN204752263U (en) * | 2015-06-19 | 2015-11-11 | 中国石油大学(华东) | Detachable dissolved air releaser |
| CN108946969A (en) * | 2018-06-08 | 2018-12-07 | 广州资源环保科技股份有限公司 | A kind of aeration system based on micro-nano bubble |
Non-Patent Citations (1)
| Title |
|---|
| 肖莹: "射流式增氧装置的试验研究", 《中国优秀硕士学位论文全文数据库 农业科技辑》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111747546A (en) * | 2020-07-15 | 2020-10-09 | 合肥济坤环保科技有限责任公司 | Intelligent pure oxygen dissolved gas water body reoxygenation technology and equipment |
| CN115108621A (en) * | 2021-03-23 | 2022-09-27 | 中国科学院上海高等研究院 | Preparation device and method of high-oxygen water |
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Application publication date: 20190329 |