CN111545035A - High-efficiency gas-liquid physicochemical reaction device - Google Patents
High-efficiency gas-liquid physicochemical reaction device Download PDFInfo
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- CN111545035A CN111545035A CN202010407069.1A CN202010407069A CN111545035A CN 111545035 A CN111545035 A CN 111545035A CN 202010407069 A CN202010407069 A CN 202010407069A CN 111545035 A CN111545035 A CN 111545035A
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- 239000007788 liquid Substances 0.000 title claims abstract description 131
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 62
- 230000007246 mechanism Effects 0.000 claims abstract description 24
- 239000000945 filler Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 abstract description 62
- 238000009423 ventilation Methods 0.000 abstract description 11
- 230000035484 reaction time Effects 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 238000012856 packing Methods 0.000 description 9
- 238000007599 discharging Methods 0.000 description 8
- 238000004090 dissolution Methods 0.000 description 6
- 241000883990 Flabellum Species 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 230000035488 systolic blood pressure Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
- B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
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- 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
Abstract
The invention relates to a high-efficiency gas-liquid physicochemical reaction device, which relates to the technical field of gas-liquid physicochemical reaction and specifically comprises a gas-liquid reaction process bin, a vapor bubble damage bin and a plurality of ventilation auxiliary pipelines, wherein a fan is arranged outside the gas-liquid reaction process bin, a gas-liquid dissolving frame is arranged in the gas-liquid reaction process bin, a gas inlet pipe communicated with the fan is arranged in the gas-liquid dissolving frame, a micron-sized vapor bubble generating mechanism communicated with the gas inlet pipe is also arranged in the gas-liquid dissolving frame, the bottom of the vapor bubble damage bin is provided with a solution discharge channel, and the top of the vapor bubble damage bin is. According to the invention, the micron-sized bubble generating mechanism is arranged in the gas-liquid dissolving frame, and gas in the gas inlet pipe enters the gas-liquid dissolving frame through the micron-sized bubble generating mechanism and contacts with the cleaning solution to form the bubbles of the liquid shell formed by wrapping the gas in the cleaning solution, so that the specific surface area contacting with the cleaning solution is increased, the reaction time of the gas and the cleaning solution is further increased, and the gas cleaning efficiency is improved.
Description
Technical Field
The invention relates to the technical field of gas-liquid physicochemical reaction, in particular to a high-efficiency gas-liquid physicochemical reaction device.
Background
Among the prior art, the device that carries out cleaning process to gas is CN205164402U discloses a exhaust treatment device as authorized bulletin number, including the water purification case and with the water pump of water purification case switch-on, the water pump other end has the gas mixing box through the inlet tube intercommunication, gas mixing box top intercommunication has the exhaust pipe and is used for the exhaust column of pumped water smoke, install the fan on the exhaust column, the fan intercommunication has the separator box, be provided with the blast pipe on the separator box, be provided with the filter screen in the blast pipe, gas mixing box middle part is provided with the overflow launder, the overflow launder intercommunication has the sedimentation tank, the sedimentation tank has the filter pond through the overflow intercommunication, communicate circulating water pipe between filter pond and the water purification case.
The above prior art solutions have the following drawbacks: when using above-mentioned device to clean gas, gas enters into the gas mixing box through the exhaust pipe and carries out the waste residue, solid matter clearance back such as granule, remaining gas is discharged by the blast pipe after reacting in the cleaning solution that gets into the separator box, this kind is through directly letting in gas cleaning solution and react the clear mode, gas is very fast through cleaning solution's speed, make the area that gas can fully contact with cleaning solution less, and then gas is shorter with cleaning solution's reaction time, lead to gaseous cleaning efficiency to be lower.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide the efficient gas-liquid physicochemical reaction device which has the advantage of improving the gas cleaning efficiency.
The above object of the present invention is achieved by the following technical solutions: the utility model provides a high-efficient gas-liquid materialization reaction device, includes gas-liquid reaction process storehouse, sets up in the damaged storehouse of bubble and the attached pipeline of ventilating that communicates the damaged storehouse of gas-liquid reaction process storehouse and bubble top, the gas-liquid reaction process storehouse is equipped with the fan outward, be equipped with gas-liquid in the gas-liquid reaction process storehouse and dissolve the frame, be equipped with the intake pipe that communicates the fan in the gas-liquid dissolves the frame, still be equipped with a plurality of layers in the gas-liquid dissolves the frame and communicate the micron order bubble generating mechanism of intake pipe, the solution discharge channel has been seted up to the bottom in the damaged storehouse of bubble, the exhaust emission pipeline has been seted up at the top in the damaged.
By adopting the technical scheme, the gas-liquid dissolving frame is internally provided with the cleaning solution for cleaning the gas, the fan is started to suck the gas to be cleaned into the gas inlet pipe, the gas in the gas inlet pipe is dispersed into the gas-liquid dissolving frame through the micron-sized bubble generating mechanism on each layer, and forms a vapor bubble which wraps the gas in a liquid shell formed by the cleaning solution after contacting with the cleaning solution, so as to increase the contact area of the gas and the cleaning solution, then the vapor bubble emerges from the liquid level of the cleaning solution and enters the vapor bubble damaged bin through the ventilation auxiliary pipeline, after the bubbles in the bubble breakage bin are broken, the gas overflows from the tail gas discharge pipeline, the cleaning solution is discharged from the solution discharge channel, the contact area between the gas and the cleaning solution is increased in the process of cleaning the gas by the whole device, and further, the reaction time between the gas and the cleaning solution is prolonged, and the gas cleaning efficiency is improved.
The present invention in a preferred example may be further configured to: the micron-sized bubble generating mechanism comprises a plurality of sintered filter rods arranged on the outer side wall of the air inlet pipe, air ducts communicated with the air inlet pipe are formed in the sintered filter rods, and a plurality of micropores communicated with the air ducts are formed in the side wall of each sintered filter rod.
Through adopting above-mentioned technical scheme, the gas in the intake pipe enters into the air duct of every sintering filter rod, and in the clean solution that enters into gas-liquid dissolution frame from the air duct through the micropore, after passing through the micropore, gas and clean solution contact formation steam pocket to wrap up gas in the liquid casing of clean solution, with the specific surface area and the reaction time of increase gas and clean solution, with the gas in the steam pocket clean, and then improve the clean efficiency that needs clean gas.
The present invention in a preferred example may be further configured to: the sintered filter rods between two adjacent layers of micron-sized bubble generating mechanisms are arranged in a mutually staggered manner.
By adopting the technical scheme, when gas is dispersed from the micropores to form bubbles, the bubbles between the two adjacent layers of micron-sized bubble generating mechanisms are formed and move to the liquid level of the cleaning solution, the collision between the bubbles is reduced, and the breakage of the bubbles can be further reduced.
The present invention in a preferred example may be further configured to: and a plurality of liquid level rods are also arranged in the gas-liquid dissolving frame and are positioned above the micron-sized bubble generating mechanism.
Through adopting above-mentioned technical scheme, through setting up the liquid level pole to add the volume of cleaning solution in dissolving the frame to the gas-liquid and control.
The present invention in a preferred example may be further configured to: and a breaking piece is arranged in the steam bubble breakage bin.
Through adopting above-mentioned technical scheme, through setting up the rupture piece for the bubble is entering into the damaged storehouse of bubble after, and the accessible rupture piece carries out the bubble and breaks, makes the gas-liquid separation of bubble, in the bubble that reduces to take clean solution passes through tail gas discharge pipeline and enters into the air, and then reducible pollution to the air.
The present invention in a preferred example may be further configured to: the rupture member includes a filler layer covering the exhaust gas discharge pipe.
Through adopting above-mentioned technical scheme, through setting up the packing layer for take the vapor bubble of cleaning solution to enter into the damaged storehouse of vapor bubble and to the in-process of exhaust emission pipeline motion, directly break behind the collision packing layer.
The present invention in a preferred example may be further configured to: the breaking piece comprises a motor arranged at the top of the damaged vapor bubble bin and fan blades arranged in the damaged vapor bubble bin, and an output shaft of the motor penetrates through the damaged vapor bubble bin and is connected with the fan blades.
Through adopting above-mentioned technical scheme, the motor starts to drive the flabellum and rotates, and the flabellum contacts with the bubble to break the bubble.
The present invention in a preferred example may be further configured to: the ventilating auxiliary pipeline penetrates into the damaged steam bubble bin, and the end part of the ventilating auxiliary pipeline, which is positioned in the damaged steam bubble bin, protrudes out of the inner bottom wall of the damaged steam bubble bin.
Through adopting above-mentioned technical scheme, after the bubble breaks, the clean solution that the bubble surface covered drips behind the interior diapire in the damaged storehouse of bubble to reduce clean solution and return to in the gas-liquid reaction process storehouse from the attached pipeline of ventilating.
The present invention in a preferred example may be further configured to: the fan adopts a low-pressure fan.
By adopting the technical scheme, the low-pressure fan is adopted to suck gas, so that the sucked gas is in a low-pressure state, and the energy consumption is favorably reduced.
The present invention in a preferred example may be further configured to: the inner bottom wall of the gas-liquid reaction process bin is provided with a support, and the gas-liquid dissolving frame is arranged on the support.
Through adopting above-mentioned technical scheme, through setting up the support, in order to dissolve the position of placing of frame in gas-liquid reaction process storehouse to the gas-liquid and fix a position, make simultaneously that the gas-liquid dissolves and leave certain space between the bottom of frame and the interior diapire in gas-liquid reaction process storehouse, after breaking in the gas-liquid reaction process storehouse in order to reduce partial bubble, the bottom that the clean solution that drips and gas-liquid dissolved the frame contacts, and then reducible when dissolving the frame to the gas-liquid, carry out the clean solution to the air in from the gas-liquid reaction process storehouse, and then reducible pollution to the air.
In summary, the invention includes at least one of the following beneficial technical effects:
1. the micron-sized bubble generating mechanisms are arranged in the gas-liquid dissolving frame, gas in the gas inlet pipe enters the gas-liquid dissolving frame in a dispersed mode through the micron-sized bubble generating mechanisms on each layer and contacts with the cleaning solution to form bubbles of a liquid shell formed by wrapping the gas in the cleaning solution, so that the contact area of the bubbles with the cleaning solution is increased, the reaction time between the gas and the cleaning solution is further prolonged, and the gas cleaning efficiency is improved;
2. after the gas passes through the micropores, the gas is contacted with the cleaning solution to form bubbles, so that the gas is wrapped in the liquid shell of the cleaning solution, the specific surface area and the reaction time of the gas and the cleaning solution are increased, the gas in the bubbles is cleaned, and the cleaning efficiency of the gas needing to be cleaned is improved.
Drawings
Fig. 1 is a schematic structural diagram of a first embodiment of the present invention.
Fig. 2 is a first schematic structural diagram of a gas-liquid dissolving frame in a first embodiment of the invention.
Fig. 3 is a schematic structural diagram of a gas-liquid dissolving frame in the first embodiment of the invention.
Fig. 4 is a partially enlarged schematic view of a portion a in fig. 2.
Fig. 5 is a schematic view of an internal structure of the bubble breakage bin according to the first embodiment of the present invention.
Fig. 6 is a schematic view of the internal structure of the bubble breakage bin in the second embodiment of the present invention.
In the figure, 1, a gas-liquid reaction process bin; 11. a fan; 12. an air inlet pipe; 13. a support; 131. a cross bar; 132. a vertical rod; 2. a damaged bubble bin; 21. a solution discharge channel; 22. a tail gas discharge pipeline; 23. an air outlet space; 3. an air-breathing auxiliary duct; 4. a gas-liquid dissolving frame; 41. a liquid level lever; 5. a micron-sized bubble generating mechanism; 51. sintering the filter stick; 511. an air duct; 512. micropores; 6. a rupture member; 7. a filler layer; 8. a motor; 9. a fan blade; 10. a controllable medicine adding mechanism; 101. a mixing pump; 102. a feed pipe; 103. a discharge pipe; 104. a drainage tube; 105. and a feeding bin.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
The first embodiment is as follows:
referring to fig. 1, the high-efficiency gas-liquid physicochemical reaction device disclosed by the invention comprises a gas-liquid reaction process bin 1, a bubble damage bin 2 arranged above the gas-liquid reaction process bin 1, and a plurality of auxiliary ventilation pipelines 3 communicating the gas-liquid reaction process bin 1 and the bubble damage bin 2.
Referring to fig. 1 and 2, a cuboid gas-liquid dissolving frame 4 is placed on the side wall of the gas-liquid reaction process bin 1 far away from the bubble damage bin 2, a cuboid gas inlet pipe 12 is fixedly connected in the gas-liquid dissolving frame 4, two ends of the gas inlet pipe 12 in the length direction are fixedly connected to the inner side wall of the gas-liquid dissolving frame 4 in the width direction, and the center line of the gas inlet pipe 12 in the width direction and the center line of the gas-liquid dissolving frame 4 in the width direction are overlapped; the top of the gas-liquid reaction process bin 1 is fixedly connected with a low pressure fan 11 communicated with an air inlet pipe 12, the low pressure fan 11 is used for sucking gas to be cleaned into the air inlet pipe 12, the air pressure of the low pressure fan 11 is preferably 0.5KPa-4KPa in the embodiment, the low pressure fan 11 is used for sucking gas, energy consumption can be reduced, and the amount of gas which can be absorbed is larger.
A controllable medicine adding mechanism 10 is arranged outside the gas-liquid reaction process bin 1, the controllable medicine adding mechanism 10 comprises a mixing pump 101, a feeding pipe 102 communicated with a feeding hole of the mixing pump 101 and a discharging pipe 103 communicated with a discharging hole of the mixing pump 101, one end, far away from the mixing pump 101, of the discharging pipe 103 is communicated to a gas-liquid dissolving frame, a plurality of drainage pipes 104 are communicated on the side wall of the feeding pipe 102, and one end, far away from the mixing pump 101, of each drainage pipe 104 is communicated with a corresponding feeding bin 105; when cleaning solution is introduced into the gas-liquid dissolving frame, the mixing pump 101 can be started, raw materials in the feeding bins 105 enter the feeding pipe 102 through the drainage pipe 104, then are fed into the mixing pump 101 to be mixed, and are fed into the gas-liquid dissolving frame through the discharging pipe 103.
Referring to fig. 2 and 3, a plurality of micron-sized bubble generating mechanisms 5 communicated with the air inlet pipe 12 are arranged between the outer side wall of the air inlet pipe 12 in the length direction in the air-liquid dissolving frame 4 and the inner side wall of the air-liquid dissolving frame 4 in the length direction, in the embodiment, the micron-sized bubble generating mechanisms 5 are preferably two layers from top to bottom, each layer of micron-sized bubble generating mechanism 5 comprises a plurality of sintered filter rods 51 fixedly connected to the outer side wall of the auxiliary ventilation pipeline 3, and the sintered filter rods 51 between the two adjacent layers of micron-sized bubble generating mechanisms 5 are arranged in a mutually staggered manner; in this embodiment, the plurality of sintered filter rods 51 of each layer are uniformly arranged along the length direction of the air inlet pipe 12 or the sintered filter rods 51 of each layer are divided into two groups, and the length of each group of sintered filter rods 51 is firstly lengthened and then shortened along the length direction of the air inlet pipe 12, so that each group of sintered filter rods 51 forms a fan shape; a plurality of liquid level rods 41 are fixed between the inner side walls in the length direction in the gas-liquid dissolving frame 4, and each liquid level rod 41 is positioned above the micron-sized bubble generating mechanism 5.
Referring to fig. 2 and 4, an air duct 511 communicated with the air auxiliary duct 3 is arranged in the sintered filter stick 51 along the axial direction, a plurality of micropores 512 communicated with the air duct 511 are arranged on the side wall of the sintered filter stick 51, and the aperture of each micropore 512 is less than or equal to 5 μm; when the gas to be cleaned is cleaned, the cleaning solution is added into the gas-liquid dissolving frame 4 until the cleaning solution covers all the sintered filter rods 51, the low-pressure fan 11 is started and sucks the gas to be cleaned into the auxiliary ventilating pipeline 3, and then the gas to be cleaned enters the ventilating duct 511 of the sintered filter rods 51 and is dispersed into the gas-liquid dissolving frame 4 through the micropores 512.
Gas and the gas-liquid dissolve the cleaning solution in the frame 4 and contact, form the diameter of wrapping up gas in liquid casing and be less than or equal to 5 mu m's steam bubble, liquid casing is cleaning solution in this embodiment, and make and steam bubble inside produce a materialization reaction environment that has little systolic pressure, in the environment of little systolic pressure, because liquid casing surface has tension, make gaseous molecule of gas in the steam bubble be liable to enter into liquid molecule clearance and react, make in the gas that needs to be cleaned and the cleaning solution reaction process, the specific surface area of gas and cleaning solution contact increases, and be the increase of exponential form, and then increase the reaction time between gas that needs to be cleaned and the cleaning solution, form the supersaturated of gas and dissolve, improve clear efficiency.
After the bubbles are formed and in the gas-liquid reaction process in the bubbles, the bubbles gradually move upwards and are separated from the cleaning solution and then enter the damaged bubble bin 2 through the ventilating auxiliary pipeline 3, meanwhile, in order to prolong the time for maintaining the bubbles and increase the gas-liquid physicochemical reaction time in the micro-contraction pressure environment, a chemical reagent for maintaining the bubble time is added into the cleaning solution so as to increase the surface tension coefficient of the liquid shell, the chemical reagent is preferably soap water in the embodiment, so that the bubbles can be maintained after being separated from the cleaning solution and then break after entering the damaged bubble bin 2, and the direct breakage of the bubbles after being separated from the cleaning solution is reduced.
Referring to fig. 5, a support 10 is fixedly connected to the bottom wall of the gas-liquid reaction process bin 1 below the gas-liquid dissolution frame 4, the support 10 includes two cross rods 101 and vertical rods 102 which are perpendicular to each other, two ends of the cross rods 101 and the vertical rods 102 extend and are fixed to the corresponding inner side walls of the gas-liquid reaction process bin 1, the gas-liquid dissolution frame 4 is placed on the support 10, so that a certain space is reserved between the bottom of the gas-liquid dissolution frame 4 and the inner bottom wall of the gas-liquid reaction process bin 1, and after part of bubbles are broken in the gas-liquid reaction process bin 1, the cleaning solution on the surfaces of the bubbles drops into the gas-liquid reaction process bin 1, so that the cleaning solution is prevented from contacting the bottom of the gas-liquid dissolution frame 4, and therefore, when the gas-liquid dissolution frame 4 is replaced, the cleaning solution is brought out of the gas-liquid reaction process bin.
Tail gas discharging pipe 22 has been seted up at the top in the damaged storehouse of bubble 2, solution discharge passageway 21 has been seted up to the bottom in the damaged storehouse of bubble 2, solution discharge passageway 21 is used for the intercommunication water pipe, the bubble in the gas-liquid reaction process storehouse 1 gets into in the damaged storehouse of bubble 2 through the accessory pipeline 3 of ventilating, because the bubble is through wrapping up gas in the liquid casing that is formed by cleaning solution, form water smoke after the bubble breaks in the damaged storehouse of bubble 2, gaseous this moment is in the air through tail gas discharging pipe 22 entering, cleaning solution drips on the interior diapire in the damaged storehouse of bubble 2, the rethread solution goes out and collects again after discharge passageway 21 inlet tube.
The end part of the ventilation auxiliary pipeline 3 close to the steam bubble damage bin 2 penetrates through the steam bubble damage bin 2, and the end part of the ventilation auxiliary pipeline 3 located in the steam bubble damage bin 2 protrudes out of the inner bottom wall of the steam bubble damage bin 2, so that when the cleaning solution drops on the inner bottom wall of the steam bubble damage bin 2 after the steam bubble is broken, the cleaning solution is reduced from returning to the gas-liquid reaction process bin 1 from the ventilation auxiliary pipeline 3.
The broken steam bubble bin 2 is also internally provided with a breaking piece 6, the breaking piece 6 comprises a packing layer 7 for covering a tail gas discharge pipeline 22, the side wall of the packing layer 7 is fixed on the inner side wall of the broken steam bubble bin 2, and an air outlet space 23 is left between the packing layer 7 and the tail gas discharge pipeline 22, the packing layer 7 is preferably a mesh cloth in the embodiment, the arrangement of the packing layer 7 enables the bubbles with the cleaning solution to be subjected to external force rupture through the contact with the packing layer 7 after entering the damaged chamber 2 of the bubbles, further, the gas and the liquid of the bubbles are separated, the gas enters the gas outlet space 23 from the gap of the packing layer 7 and is discharged from the tail gas discharge pipeline 22, the cleaning solution drops on the inner bottom wall of the bubble damage bin 2, so that when the bubbles do not automatically break after entering the bubble damage bin 2, the cleaning solution is brought into the air through the exhaust gas discharge pipe 22, and thus the pollution to the air can be reduced.
Example two:
referring to fig. 6, a high-efficiency gas-liquid physicochemical reaction device, based on a further improvement of the inside of the vapor bubble damage bin 2 in the first embodiment, comprises a gas-liquid reaction process bin 1, the vapor bubble damage bin 2 arranged above the gas-liquid reaction process bin 1, and a plurality of auxiliary ventilation pipelines 3 communicating the gas-liquid reaction process bin 1 and the vapor bubble damage bin 2.
Tail gas discharging pipe 22 has been seted up at the top in the damaged storehouse of bubble 2, solution discharge passageway 21 has been seted up to the bottom in the damaged storehouse of bubble 2, solution discharge passageway 21 is used for the intercommunication water pipe, the bubble in the gas-liquid reaction process storehouse 1 gets into in the damaged storehouse of bubble 2 through the accessory pipeline 3 of ventilating, because the bubble is through wrapping up gas in the liquid casing that is formed by cleaning solution, form water smoke after the bubble breaks in the damaged storehouse of bubble 2, gaseous this moment is in the air through tail gas discharging pipe 22 entering, cleaning solution drips on the interior diapire in the damaged storehouse of bubble 2, the rethread solution goes out and collects again after discharge passageway 21 inlet tube.
The end part of the ventilation auxiliary pipeline 3 close to the steam bubble damage bin 2 penetrates through the steam bubble damage bin 2, and the end part of the ventilation auxiliary pipeline 3 located in the steam bubble damage bin 2 protrudes out of the inner bottom wall of the steam bubble damage bin 2, so that when the cleaning solution drops on the inner bottom wall of the steam bubble damage bin 2 after the steam bubbles are broken, the cleaning solution is reduced and returns to the gas-liquid reaction process bin 1 from the ventilation auxiliary pipeline 3.
Still be equipped with the rupture piece 6 in the damaged storehouse of bubble 2, rupture piece 6 includes the motor 8 of fixed connection in the damaged storehouse of bubble 2 top, set up flabellum 9 in the damaged storehouse of bubble 2, motor 8's output shaft is worn to establish to the damaged storehouse of bubble 2 in and fixed connection on flabellum 9, the bubble is after entering into the damaged storehouse of bubble 2, accessible starter motor 8 drives flabellum 9 and rotates and touch the bubble, it breaks to carry out external force to the bubble, and then make the gas-liquid separation of bubble, in order to reduce the bubble and enter into the air through tail gas discharge pipeline 22 when not automatic breakage after entering into the damaged storehouse of bubble 2, and then reducible pollution to the air.
The embodiments of the present invention are preferred embodiments of the present invention, and the scope of the present invention is not limited by these embodiments, so: all equivalent changes made according to the structure, shape and principle of the invention are covered by the protection scope of the invention.
Claims (10)
1. The utility model provides a high-efficient gas-liquid materialization reaction unit which characterized in that: including gas-liquid reaction process storehouse (1), set up in damaged storehouse of bubble (2) and the intercommunication above gas-liquid reaction process storehouse (1) the auxiliary pipeline (3) of ventilating in damaged storehouse of bubble (2) and gas-liquid reaction process storehouse (1), gas-liquid reaction process storehouse (1) is equipped with fan (11) outward, be equipped with gas-liquid in the gas-liquid reaction process storehouse (1) and dissolve frame (4), be equipped with intake pipe (12) of intercommunication fan (11) in gas-liquid dissolves frame (4), still be equipped with a plurality of layers of intercommunication in the gas-liquid dissolves frame (4) micron order bubble generation mechanism (5) of intake pipe (12), solution discharge passageway (21) have been seted up to the bottom in damaged storehouse of bubble (2), tail gas discharge pipeline (22) have been seted up to the top in damaged storehouse of bubble (2).
2. The efficient gas-liquid physicochemical reaction device according to claim 1, characterized in that: the micron-sized vapor bubble generating mechanism (5) comprises a plurality of sintered filter sticks (51) arranged on the outer side wall of the air inlet pipe (12), air passages (511) communicated with the air inlet pipe (12) are formed in the sintered filter sticks (51), and a plurality of micropores (512) communicated with the air passages (511) are formed in the side wall of each sintered filter stick (51).
3. The efficient gas-liquid physicochemical reaction device according to claim 2, characterized in that: the sintered filter rods (51) between two adjacent layers of micron-sized bubble generating mechanisms (5) are arranged in a mutually staggered manner.
4. The efficient gas-liquid physicochemical reaction device according to claim 2, characterized in that: a plurality of liquid level rods (41) are further arranged in the gas-liquid dissolving frame (4), and the liquid level rods (41) are located above the micron-sized bubble generating mechanism (5).
5. The efficient gas-liquid physicochemical reaction device according to claim 1, characterized in that: and a breaking piece (6) is arranged in the bubble breakage bin (2).
6. The efficient gas-liquid physicochemical reaction device according to claim 5, characterized in that: the rupture element (6) comprises a filler layer (7) covering the exhaust gas discharge duct (22).
7. The efficient gas-liquid physicochemical reaction device according to claim 5, characterized in that: the breaking piece (6) comprises a motor (8) arranged at the top of the damaged steam bubble bin (2) and fan blades (9) arranged in the damaged steam bubble bin (2), and an output shaft of the motor (8) penetrates through the damaged steam bubble bin (2) and is connected with the fan blades (9).
8. The efficient gas-liquid physicochemical reaction device according to claim 1, characterized in that: the ventilating auxiliary pipeline (3) penetrates into the damaged steam bubble bin (2), and the end part of the ventilating auxiliary pipeline (3) positioned in the damaged steam bubble bin (2) protrudes out of the inner bottom wall of the damaged steam bubble bin (2).
9. The efficient gas-liquid physicochemical reaction device according to claim 1, characterized in that: the fan (11) adopts a low-pressure fan (11).
10. The efficient gas-liquid physicochemical reaction device according to claim 1, characterized in that: the inner bottom wall of the gas-liquid reaction process bin (1) is provided with a support (10), and the gas-liquid dissolving frame (4) is arranged on the support (10).
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010407069.1A CN111545035B (en) | 2020-05-14 | 2020-05-14 | High-efficiency gas-liquid physicochemical reaction device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010407069.1A CN111545035B (en) | 2020-05-14 | 2020-05-14 | High-efficiency gas-liquid physicochemical reaction device |
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| CN111545035B CN111545035B (en) | 2022-07-12 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115121191A (en) * | 2022-07-13 | 2022-09-30 | 重庆大学 | Preparation of PEDOT by gas-liquid two-phase reaction: PSS device and method |
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| CN111545035B (en) | 2022-07-12 |
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Denomination of invention: Efficient gas-liquid physicochemical reaction device Effective date of registration: 20231204 Granted publication date: 20220712 Pledgee: Zhejiang Tailong Commercial Bank Co.,Ltd. Taizhou Technology Branch Pledgor: Taizhou Huajie Environmental Protection Technology Co.,Ltd. Registration number: Y2023980068958 |