阅读说明：本技术 一种气体裂泡净化装置、系统、方法及应用 (Gas cracking bubble purification device, system, method and application ) 是由 曾德邻 曾固 于 2020-03-29 设计创作，主要内容包括：一种气体裂泡净化装置、系统、方法及应用,将待净化气体以汆入方式引入水贮体(100),水贮体(100)内部署的裂泡结构(200)使初始气泡被充分裂解或碎化,气泡中气体获得足够释放与水接触,由水与裂泡结构(200)针对气体杂质的拦截、浸润、溶解、吸收、吸附等净化作用,或者还通过级联净化的后级有区别净化获得超高净化效果；采用独有气尘分离与尘自降,不借助其它专用脱尘装置的连续可持久排渣甚至包括浮尘分离与收集技术,降低脱尘成本；可应用于工业气体、生产现场气体、有毒有害气体、臭气、生化气体、单纯空气等净化处理,以及送新风等领域。(A gas cracking and bubble purifying device, system, method and application, the gas to be purified is led into a water storage body (100) in a quick boiling mode, a cracking and bubble structure (200) arranged in the water storage body (100) leads the initial bubbles to be cracked or smashed fully, the gas in the bubbles is released enough to be contacted with water, the water and the cracking and bubble structure (200) have the purifying functions of intercepting, infiltrating, dissolving, absorbing, adsorbing and the like aiming at gas impurities, or the ultrahigh purifying effect is obtained through the subsequent differential purification of the cascade purification; the dust removal cost is reduced by adopting unique gas-dust separation and dust self-falling, and continuous and durable slag discharge without other special dust removal devices, even floating dust separation and collection technologies; can be applied to the fields of purification treatment of industrial gas, production site gas, toxic and harmful gas, odor, biochemical gas, pure air and the like, fresh air supply and the like.)

The utility model provides a gaseous bubble purifier that splits which characterized in that: the device comprises a water storage body, wherein a crack bubble structure which is completely or partially immersed by a liquid purification material is arranged in the water storage body, and micropores or microgaps used for cracking or crushing the gas to be purified are formed in the crack bubble structure.

2. A gas bubble purification apparatus according to claim 1, wherein: the liquid purification material comprises water.

3. A gas bubble purification apparatus according to claim 2, wherein: the liquid purification material further comprises modified water.

4. A gas bubble purification apparatus according to claim 1, wherein: the said structure of the said crack bubble is composed of the same/different materials or micro-porous/micro-gap structure combination.

5. A gas bubble purification apparatus according to claim 1, wherein: the micropores or microgaps are ordered micropores or microgaps or disordered micropores or microgaps.

6. A gas bubble purification apparatus according to claim 1, wherein: the said crack structure has the function of purifying gas.

7. A gas bubble purification apparatus according to claim 1, wherein: the water storage body is internally provided with a multiple-crack foam structure.

8. The gas bubble purification apparatus of claim 7, wherein: the multiple-split bubble structures respectively have the same or different micropore densities.

9. The gas bubble purification apparatus of claim 7, wherein: the density of the micropores of the multi-crack structure increases along the ascending direction of the gas to be purified.

10. A gas bubble purification apparatus according to claim 1, wherein: the shape of the crack bubble structure is one or more of a flat plate structure, a pyramid structure and a bidirectional pyramid structure.

11. A gas bubble purification apparatus according to claim 10, wherein: the cracking bubble structure adopts a rigid thin plate structure.

12. A gas bubble purification apparatus according to claim 10, wherein: the cracking bubble structure is a net body material structure.

13. A gas bubble purification apparatus according to claim 10, wherein: the cracking foam structure is arranged in the water storage body in a horizontal mode, a single-side inclined mode, an opposite-side staggered inclined mode, a straight-falling mode or a multiple-superposition suspension mode or a plurality of modes.

14. A gas bubble purification apparatus according to claim 13, wherein: the water storage body is characterized in that a fixing structure for placing a multiple-crack foam structure is arranged on the inner side wall of the water storage body, and the fixing structure is one or more of a single-side inclined slot, an opposite-side staggered inclined slot, a hanging rod support table or a step-shaped shelf strip or a smooth surface structure.

15. A gas bubble purification apparatus according to claim 1, wherein: the structure type of the water storage body is one or a combination of more of civil engineering structure type, steel structure type and engineering plastics.

16. A gas bubble purification apparatus according to claim 1, wherein: the water storage body is internally provided with a cracking bubble purifying chamber, the cracking bubble structure is arranged in the cracking bubble purifying chamber, and the gas to be purified enters the cracking bubble purifying chamber from the lower part of the cracking bubble structure.

17. The gas bubble purification apparatus of claim 16, wherein: and the water storage body is also internally provided with an air introducing chamber, and the gas to be purified enters the cracked bubble purifying chamber through an air guide structure arranged in the air introducing chamber.

18. A gas bubble purification apparatus according to claim 17, wherein: a top cover is further arranged above the water storage body, and an air outlet channel is arranged on the top cover.

19. A gas bubble purification apparatus according to claim 18, wherein: the air outlet channel is communicated with the cracking bubble purifying chamber and the air introducing chamber.

20. A gas bubble purification apparatus according to claim 18, wherein: the air outlet channel is only communicated with the cracking bubble purifying chamber.

21. A gas bubble purification apparatus according to claim 20, wherein: and the top cover is provided with a gas external connection channel which is independently communicated with the gas introducing chamber.

22. A gas bubble purification apparatus according to claim 17, wherein: and a transverse gas guide structure is arranged in the gas introducing chamber so that the gas to be purified transversely expands in the gas advancing direction before entering the cracking and foaming purifying chamber.

23. A gas bubble purification apparatus according to claim 22, wherein: and a longitudinal gas guide structure is arranged above the gas outlet of the transverse gas guide structure, so that the gas to be purified after being transversely expanded is longitudinally expanded along the gas advancing direction.

24. A gas cracking and bubble purifying system is characterized in that: the gas cracking and foaming device as claimed in any one of claims 1 to 23, further comprising a gas introducing device for delivering gas to be purified into the gas cracking and foaming device and an exhaust device for exhausting purified gas from the gas cracking and foaming device.

25. The gas bubble purification system of claim 24, wherein: the slag discharging device comprises a slag collecting structure arranged at the bottom of the water storage body, a mechanical inner slag discharging mechanism is arranged in the slag collecting structure, and the mechanical inner slag discharging mechanism is used for discharging sediments in the slag collecting structure from the inside of the water storage body.

26. The gas bubble purification system of claim 25, wherein: the mechanical material conveying device is matched with the mechanical inner slag discharging mechanism and used for transferring the sediments discharged by the mechanical inner slag discharging mechanism.

27. The gas bubble purification system of claim 24, wherein: still include the moisturizing device, the moisturizing device includes the moisturizing pipe, the moisturizing pipe with the internal intercommunication of water storage.

28. The gas bubble purification system of claim 24, wherein: the water storage device also comprises a drainage device, wherein the drainage device comprises a drainage pipe arranged at the bottom of the water storage body.

29. The gas bubble purification system of claim 24, wherein: also comprises a scum discharging and collecting device.

30. The gas bubble purification system of claim 24, wherein: also comprises an auxiliary agent adding device.

31. The gas bubble purification system of claim 24, wherein: also comprises a sampling inspection device for inspecting the purified water and gas.

32. The gas bubble purification system of claim 24, wherein: the system also comprises a control and operation system.

33. The gas bubble purification system of claim 24, wherein: also comprises a purified gas optimizing device.

34. The gas bubble purification system of claim 24, wherein: also comprises a system for recycling waste water and waste residue after gas purification.

35. The utility model provides a gaseous bubble clean system that splits of tandem type which characterized in that: a plurality of gas bubble purification systems according to any of claims 24-34 arranged in series.

36. The utility model provides a gaseous bubble clean system that splits of cluster which characterized in that: a plurality of cascaded gas cracking bubble purification systems of claim 35 are adopted and arranged in parallel.

37. The clustered gas cracking and bubbling system according to claim 36, further comprising a gas input distribution valve for gas to be purified, wherein the gas input distribution valve for gas to be purified has a main input port at one end and a plurality of branch gas transmission ports at the other end, and the branch gas transmission ports are connected with the gas purification device through pipelines.

38. A gas cracking bubble purification method is characterized in that: the method comprises the following steps:

the method comprises the following steps: deploying a gas purification apparatus as claimed in any one of claims 1 to 23;

introducing gas to be purified into the front end of a crack bubble structure arranged in the water storage body in a quick-boiling mode;

step three: the gas to be purified which is introduced into the water storage body is subjected to at least one of cracking or fragmentation of the cracking structure and is purified by the liquid purification material;

step four: and discharging the purified gas from the water reservoir.

39. The gas bubble purification method of claim 38, wherein: the gas purification device enables the waste residue generated in the cracking and foaming purification process of the gas to be purified containing the waste residue to automatically precipitate and collect at the bottom of the water storage body, and the waste residue is transferred out of the water storage body through the slag discharge device.

40. The gas bubble purification method of claim 38, wherein: further comprises the following steps: and transferring, processing and utilizing the purified wastewater/waste residue.

41. The gas bubble purification method of claim 38, wherein: the gas purification devices are arranged in series to form a cascade gas cracking bubble purification system.

42. The gas bubble purification method of claim 41, wherein: the gas purification device is deployed by arranging a plurality of cascaded gas cracking and bubble purification systems in parallel to form a clustered gas cracking and bubble purification system.

43. A gas bubble cleaning method according to claim 41 or 42, wherein: the adjacent gas purification devices are communicated through interstage water replenishing pipes in sequence to form a water replenishing mode from back to front step by step, and the last-stage gas purification device is communicated with the water replenishing pipes to directly replenish water.

44. Use of a gas bubble cleaning method according to any one of claims 38 to 43.

45. A household cracking bubble air cleaner using the gas cleaning apparatus according to any one of claims 1 to 23, wherein: the outer side of the water storage body is provided with an outer air inlet, an inner air guiding outlet is arranged below the bubble cracking structure, the outer air inlet is communicated with the inner air guiding outlet through a built-in air guiding channel, an opening in the upper portion of the water storage body is provided with a fan, and an air outlet of the fan is arranged outwards.

46. The domestic crack bubble air purifier of claim 45, wherein: a water drainage hole is arranged at the bottom of the water storage body, and a water plug is configured at the water drainage hole.

47. A domestic cracking bubble air cleaner according to claim 45 or 46, wherein: the split bubble structure is a multiple cone-shaped split bubble structure body.

48. A domestic cracking bubble air cleaner according to claim 45 or 46, wherein: the air outlet of the fan is provided with a purified air outlet for radial air outlet.

49. A gas bench-type bubble scrubber using the gas scrubber apparatus as recited in any one of claims 1-23, wherein: a circumferential air duct communicated with an air guide pipe is arranged below the water storage body, an air outlet leading to the interior of the water storage body is formed in the circumferential air duct, and the air outlet is arranged at the bottom or near the bottom of the cracking bubble structure; the water storage device is characterized in that a cover body is further arranged at an opening in the upper portion of the water storage body, a fan is mounted on the cover body, and an air outlet of the fan is arranged outwards.

50. The gas table type cracking bubble scrubber of claim 49, wherein: the upper part of the water storage body is provided with a fixed connection device matched with the cover body, so that the cover body and the opening of the water storage body are conveniently opened and hermetically and fixedly connected.

51. The gas table type cracking bubble scrubber of claim 49, wherein: the side surface of the water storage body is also provided with an injection port of water/additive, and the bottom of the water storage body is also provided with a discharge port of water/sediment.

Technical Field

The invention relates to the technical field of gas purification, in particular to a gas cracking bubble purification device, system, method and application.

Background

Common gas purification such as industrial gas purification, production site gas purification, poisonous and harmful gas purification, odor purification, biochemical gas purification, pure air purification, fresh air supply and the like relates to various aspects of production, life, society and the like, relates to various fields such as environment, health, safety, quality and the like, and is an indispensable industry for society as a whole. Meanwhile, the gas purification technology is also a technical door which can deeply influence the social operation.

The gas to be purified has various objects and types, different gas purification purposes and different purification requirements, so that the existing gas purification methods have various types.

Common gas purification methods fall into a large category: physical methods, chemical methods, biological methods. Specifically, there are filtration, absorption, adsorption, condensation, catalytic conversion, combustion, membrane separation, biological purification, and the like.

The gas purification method has a plurality of defects in the practical application process.

Taking wet purification as an example, wet purification is a common purification method for gas mixtures and is classified into pumpless water curtain purification, venturi water curtain purification, water-spinning purification, etc. according to the purification flow and structure. The basic principle is to use a water film (water curtain) formed by some method on the dust-containing gas impacting the inner wall of the dust remover or other special components. The purge gas object contacts or passes through a water curtain (water curtain) causing dust to be captured by the water film (water curtain). The typical wet purification process integrates two forms of water bath and spraying, firstly, the suction force of a high-pressure centrifugal fan is utilized to press dust-containing gas into a water tank filled with water with a certain height, and partial dust is adsorbed in the water through the water bath; after the uniform distribution and the flow division, the gas flows from bottom to top, and the high-pressure spray head sprays water mist from top to bottom to collect the rest dust particles; in the dust removing process, part of gaseous pollutants can be removed, so that the purpose of gas purification is achieved. The method can not realize the full combination of the dust-containing gas and the water film, so that a considerable part of the dust-containing gas can not be effectively purified.

Still more typical wet purification methods involve a water purification method of "pressing a dust-containing gas into a water tank containing water at a certain height, and adsorbing part of dust in the water by a water bath"; however, the core and main purification method of the purification method is to utilize the 'downward spraying of water mist to collect the rest of dust particles'. However, the purpose of the "water bath" is only to "adsorb part of the dust in the water through the water bath", and a technical means for sufficiently and efficiently treating the gas wrapped in the bubbles is lacked; the remaining part of the particles are collected by the 'sprayed water mist', and the water mist is not compact, so that bubbles or particles which are not purified by the water mist exist in the contact of the rising gas and the water mist, and the overall purification efficiency and effect are limited.

Taking the boiler smoke dust gas purification technology as an example, the technology comprises an indispensable dust removal technology, the practical dust removal technology is also multiple, the typical and widely applied dust removal technology is a cloth bag dust removal technology, the limiting factor of the cloth bag dust removal method is abandoned, and the defects that the dust removal operation cannot be continuously carried out and the energy consumption in the dust removal process is high are sufficient for the application of the dust removal technology.

For most gas purification technologies, there are the following: the method has the advantages that restrictive conditions exist for the object to be purified, clear index requirements are provided for the temperature, humidity, dust content, charge condition, corrosiveness, explosiveness and the like of the object to be purified, and most gas purification methods are not suitable for purifying high-temperature, high-humidity, high-dust content, high-charge, corrosive and explosive gases.

Other disadvantages are: long purification process, complex equipment structure, high energy consumption, large steel consumption, large occupied area, high requirement on anti-corrosion treatment, high operation and maintenance difficulty, high operation cost and the like.

No matter how complicated the gas purification method is, it can be generalized to three major targets, namely: the third category is the purification of the gas to be purified for both the dust-containing substances and the gaseous pollutants. All gas purification methods develop their specific purification measures around these three types of gas purification targets.

However, no practical gas purification technology which realizes broad spectrum, universality, high efficiency, reliability and economy has been found so far.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and those skilled in the art can also obtain other drawings according to the drawings without creative efforts.

FIG. 1 is a schematic view of a gas purification device with a single-side inclined hinge-mounted triple-cracking structure provided by the invention;

FIG. 2 is a schematic view of a slab-type single-side hinge obliquely-arranged bulb structure;

FIG. 3 is a schematic view of a collapsed bubble structure of a plate-configuration drop-through apparatus;

FIG. 4 is a schematic view of a pyramidal structure of a blister;

FIG. 5 is a schematic view of a bi-directional pyramid-shaped structure of a blister;

FIG. 6 is a schematic diagram of a multi-plate structure with split bubble structures arranged in a staggered and inclined manner on opposite sides;

FIG. 7 is a schematic view of a multiple pyramid configuration of a collapsed bubble structure stacked suspension arrangement;

FIG. 8 is a schematic view (one) of a single-side hinged oblique slot mounting bar of a multi-plate structure of a split-bubble structure;

FIG. 9 is a schematic view (two) of a single-side hinged oblique slot mounting bar of a multi-plate structure of a split-bubble structure;

FIG. 10 is a schematic view (one) of a multi-plate structure with a hinged and inclined opposite sides;

FIG. 11 is a schematic diagram (II) of a multi-plate structure with a hinged and inclined opposite sides;

FIG. 12 is an enlarged view taken at A in FIG. 11;

FIG. 13 is a schematic view of multiple pyramid-shaped split bubble structure multiple-stacked suspension arrangement

FIG. 14 is a schematic view of a multi-pyramid shaped bulb assembly;

FIG. 15 is a schematic view (one) of a straight-falling stepped shelf strip with a multi-bidirectional pyramid-shaped bubble splitting structure;

FIG. 16 is a schematic view (II) of a straight-falling step-type shelf with a multi-bidirectional pyramid-shaped bubble splitting structure;

FIG. 17 is an enlarged view at B in FIG. 16;

FIG. 18 is a schematic view (one) of a multi-bi-directional pyramid-shaped structure of a crack bubble placed on a step-shaped shelf;

FIG. 19 is a schematic view (II) of a multi-layer bi-directional pyramid-shaped structure of a crack bubble placed on a step-shaped shelf;

FIG. 20 is a schematic view (III) of a multi-layer bi-directional pyramid-shaped crack bubble structure placed on a step-shaped shelf strip

FIG. 21 is a schematic illustration of a horizontal drop-out configuration for a cracked foam structure of a slab construction;

FIG. 22 is an enlarged view at C of FIG. 21;

FIG. 23 is a top view (one);

FIG. 24 is a schematic view of the top cover (II);

FIG. 25 is a top view (III);

FIG. 26 is a schematic top view (IV);

FIG. 27 is a schematic top view (V);

fig. 28 is a top view (six);

FIG. 29 is a schematic view of a single outlet flat port transverse gas directing structure (one);

FIG. 30 is a schematic view of the transverse gas directing structure of a single outlet flat;

FIG. 31 is a schematic view (III) of the transverse gas directing structure of a single outlet flat;

FIG. 32 is a schematic view of a transverse gas directing structure of a plurality of outlet louvers (one);

FIG. 33 is a schematic view of a transverse gas directing structure of a plurality of outlet louvers (two);

FIG. 34 is a schematic view of a longitudinal air guide structure including longitudinal air flow splitter panels;

FIG. 35 is a schematic view of a longitudinal air guide structure including longitudinal air flow splitter panels (two);

FIG. 36 is a schematic view (III) of a longitudinal air guide structure including longitudinal air flow splitter panels;

FIG. 37 is a schematic view (IV) of a longitudinal air guide structure including longitudinal air flow splitter vanes;

FIG. 38 is a schematic view of a longitudinal gas directing structure with a fluted panel in the form of a mesh (one);

FIG. 39 is a schematic view of a longitudinal air guide structure with a fluted panel in a mesh configuration (two);

FIG. 40 is a schematic view (III) of a longitudinal gas directing structure with a fluted panel in a mesh configuration;

FIG. 41 is an external view of a gas cleaning apparatus including a slag discharging device;

FIG. 42 is a schematic view of a cascaded cracking bubble scrubbing system provided by the present invention;

FIG. 43 is a schematic view of a cascaded cracking bubble scrubbing system provided by the present invention (two);

FIG. 44 is a schematic view (III) of a cascaded cracking bubble scrubbing system provided by the present invention;

FIG. 45 is a clustered gas cracking bubble scrubbing system provided by the present invention;

FIG. 46 is a schematic illustration (one) of the input of purge gas to the distributor valve;

FIG. 47 is a schematic view (two) of the gas to be cleaned being fed to the distribution valve;

FIG. 48 is a schematic view (III) of the gas to be cleaned being fed into the distributor valve;

FIG. 49 is a schematic view (IV) of the gas to be cleaned being fed into the distributor valve;

FIG. 50 is a schematic view of a household cracking bubble air purifier according to the present invention;

FIG. 51 is a schematic view of a household cracking bubble air purifier according to the present invention;

fig. 52 is a schematic view (three) of a household cracking bubble method air purifier provided by the invention;

FIG. 53 is a schematic view (IV) of a household cracking bubble air purifier provided by the present invention;

FIG. 54 is a schematic view of a table-type cracking bubble cleaner according to the present invention;

FIG. 55 is a schematic view of a table-type cracking bubble cleaner according to the present invention;

FIG. 56 is a schematic view (III) of a table-type cracking foam purifier provided by the present invention;

FIG. 57 is a schematic view of a table-type cracking bubble cleaner provided by the present Invention (IV);

FIG. 58 is a schematic structural view of an isothickness combination type rupture disk structure;

FIG. 59 is an exploded view of FIG. 58;

FIG. 60 is a schematic view showing the structure of a mixed combination type gas purification material;

FIG. 61 is an exploded view of FIG. 60;

FIG. 62 is an enlarged view taken at D in FIG. 1;

fig. 63 is an enlarged view at E in fig. 6.

Reference numerals:

Modes for carrying out the invention

In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

In the description of the present invention, it should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance. The terms "couple" or "couples" and the like are not restricted to physical or mechanical connections, but may include electrical connections, optical connections, and the like, whether direct or indirect.

[ term interpretation ]

Quick-boiling: and the gas to be purified is subjected to water bath purification.

The invention provides a gas cracking bubble purification device, which comprises a water storage body 100, wherein a cracking bubble structure 200 which is completely or partially immersed by liquid purification materials is arranged in the water storage body 100, and micropores or microgaps used for cracking or crushing gas to be purified are constructed on the cracking bubble structure 200.

The water reservoir 100 may be used to hold water, modified water, or other liquids having a purifying function.

In specific implementation, as shown in fig. 1, the gas to be purified is introduced into the water storage body 100, and the gas to be purified is cracked or crushed through the cracking structure 200, that is, the gas to be purified is split into a plurality of small bubbles or ultra-small bubbles, so that the gas to be purified contained in the split single bubble is significantly reduced, and the total bubble film surface area is significantly increased, so that the contact area between the split bubble and the liquid purification material is significantly increased, or the path through which the bubble passes in the liquid purification material is also extended, thereby significantly improving the effects of the liquid purification material on dissolution, absorption, adsorption and the like of harmful substances in the gas to be purified, and enhancing the effect of the liquid purification material on removing the harmful substances in the gas to be purified.

Specifically, the liquid purification material comprises water, and as the water is easy to obtain and can be repeatedly used for multiple times, the strategy of green environmental protection and sustainable development is responded, and the economic cost of the purification material can be further reduced;

preferably, the liquid purification material further comprises modified water, specifically, water is used as a purification matrix, an additive is added into the purification matrix water to modify the purification matrix water, and different additives are added into the water according to different purification objects and different purification requirements or standards: such as surfactants, adsorbents, neutralizers, conditioners, catalysts, flocculants, inhibitors, displacers, and the like.

It should be noted that the additives are only some examples, and there are many optional additives for realizing the modified water, and any additives added to realize further purification of gas can be used as the specific embodiment of the present invention.

Specifically, the breaching structure 200 is composed of the same/different materials or a micro-porous/micro-gap structure combination.

Specifically, the micropores or microgaps are ordered micropores or microgaps, or disordered micropores or microgaps.

Specifically, the crack structure 200 also has a function of purging gas.

The structure 200 of the broken bubble is a structure with micropores or microgaps, which forces the large bubbles of the gas to be purified passing through the gas purifying material to be cut or broken into a plurality of small bubbles when passing through the micropores or microgaps, so that the quantity of gas which can not be purified by contacting with water is reduced as much as possible and the contact area between the gas to be purified and the purifying material is increased as much as possible, and the rising path of the broken bubbles in the purifying material is prolonged by designing the structure with the micropores or the microgaps into a three-dimensional structure with a certain height and by means of meandering the rising path of the broken bubbles in the purifying material according to the three-dimensional structure of the structure 200 of the broken bubble, thereby promoting the contact chance between the bubbles of the gas to be purified and the purifying material to be increased;

and the gas bubbles to be purified after being crushed are re-crushed by other purification materials or the cracking bubble structure 200 in the rising process, so that the effects of the purification materials on dissolving, absorbing and adsorbing harmful substances in the gas are obviously improved, the impurities in the gas to be purified are intercepted, and the effect of the purification materials on removing the harmful substances in the gas is enhanced.

Moreover, the device also comprises a multiple-cracking-bubble structure 200, so that bubbles of the gas to be purified after being crushed are re-crushed by the gas purification material in the rising process, and the effects of the gas purification material on dissolving, absorbing, adsorbing and the like of harmful substances in the gas are obviously improved;

in addition, when the cracking structure 200 is completely or partially submerged in water, the large bubbles of the gas to be purified passing through the gas purification material are forced to be split into a plurality of small bubbles when passing through the micropores or microgaps, and the rising path of the small bubbles in the water is bent due to the path characteristics of the cracking structure 200 or the purification material, so that the contact between the gas to be purified and the water and the purification opportunity are remarkably improved;

moreover, the gas water purification effect is enhanced by considering the interception of the micropores or microgaps of the crack structure 200, or the purification effects of the crack structure 200 on the purified gas, such as interception, adsorption, dissolution, absorption and the like, for example, the adsorption effect of the activated carbon on harmful substances in the purified gas.

It is understood that the above embodiments all adopt a form of matching the bubble cracking structure 200 with water-based or wet purification, and when the bubble cracking structure 200 has the functions of bubble cracking, range extending and purification, the bubble cracking and purification of the gas to be purified can be simultaneously carried out, so as to implement the anhydrous gas purification mode.

In addition, the water base can be expanded and changed as follows, specifically, water is used as a purification matrix, and additives are added into the purification matrix water to modify the purification matrix water, so that the purification matrix water is more beneficial to removing harmful substances in gas; the additive can be a surfactant, an acid-base regulator, quicklime or quicklime water and the like.

Preferably, a multiple-cracking structure 200 is provided in the purification material water storage body 100.

In specific implementation, the cracking structure 200 may be a material used for cracking bubbles, and the cracking bubbles can increase or promote the gas purifying effect of other purifying materials, such as glass fiber bundle purifying materials, ceramic purifying materials, and the like;

the material can also be a material with functions of intercepting, absorbing, dissolving and absorbing besides functions of cracking bubbles and prolonging paths, such as an activated carbon material, a sponge material, a flexible silk material, a net material, a microporous film material and the like;

the sponge body material has both a function of cracking gas or gas flow and an adsorption function of harmful substances in the gas;

the flexible silk material can be polyvinyl acetate fiber, polypropylene fiber and the like, and can simultaneously realize the functions of cracking bubbles of gas or gas flow and adsorbing harmful substances in the gas;

the active carbon micropore or micropore material can be a formed active carbon micropore or micropore material, a packaged granular active carbon material, an active carbon fiber and the like, can crack bubbles of gas or airflow, and can effectively adsorb harmful substances in the gas;

the rupturing structure 200 may be, but is not limited to, a mesh material that can rupture a gas or gas flow, and also can serve as a skeleton or outer wrap of a flexible silk material;

the bubble-splitting structure 200 may be, but is not limited to, a microporous film material that combines a bubble-splitting function for gas or gas flow and an interception function for harmful substances in the gas.

The rupturing structure 200 can be composed of, but not limited to, the same material combination or different material combinations as described above, or the same micro-pore/micro-gap structure combination or different micro-pore structure combinations;

it is understood that combinations of different pore/micro-gap structures of the same material and combinations of the same pore/micro-gap structures of different materials may be considered as embodiments of the present invention.

It should be noted that each stage of the split-bubble structure 200 may have the same/different structure of the split-bubble structure 200, for example, the upper layer is made of activated carbon material, the lower layer is made of ceramic purifying material, etc., and the split-bubble structures 200 of the upper and lower layers may also have the same/different micro/micro gap structures or the split-bubble structures 200 made of materials, for example, the lower layer is made of straight micro/micro gap structure, and the upper layer is made of inclined micro/micro gap structure, etc., and the description of the structural features of the split-bubble structure 200 is only a partial example, and other specific embodiments are possible, and any method of combining and matching different types of split-bubble structures 200 or changing the single-layer or multi-layer multiple structures can be taken as the specific embodiment of the present invention.

Preferably, the multiple burst structures are respectively composed of the same/different burst structures 200.

Preferably, the cleaning effect of the blister structure 200 increases progressively in the direction of travel of the gas to be cleaned.

In specific implementation, the combination mode of the split-bubble structure 200 may also be different micro-pore/micro-gap structures of the same material to form a combination of the split-bubble structures 200 with different purification efficiencies, or the same micro-pore/micro-gap structures of different materials to form a combination of the split-bubble structures 200 with different purification efficiencies; or a combination of different microporous/micro-gap structures of different materials. By combining the burst structure 200 in the above manner, the gas burst structure 200 having different purification efficiencies can be obtained.

As shown in fig. 58-61, different combinations of embodiments of the rupturing structure 200 are provided.

It can be understood that the cracking bubble structure 200 and the combination thereof with different purification efficiencies as described above can be applied to the hookah as well, and by adopting the purification materials with different purification efficiencies and the combination thereof, a hookah with a self-selection of the purification degree of the smoke can be obtained;

it should be noted that the above description of the combination of gas purification materials is only a few examples, and not limited to the combination according to the purification efficiency or the combination according to the gradient size, and all other examples obtained by those skilled in the art without any inventive work are within the scope of the present invention.

Preferably, as shown in fig. 1, a multiple burst structure 200 is provided in the water storage body 100.

Specifically, the multiple structure of broken bubbles 200 respectively have the same or different density of micropores.

Preferably, the density of the micropores of the multiple-cracking bubble structure is increased progressively along the ascending direction of the gas to be purified, which is beneficial to improving the gas purification effect.

Specifically, the shape of the crack bubble structure is one or more of a flat plate structure, a pyramid structure and a bidirectional pyramid structure.

In specific implementation, the shape of the split-bubble structure 200 shown in fig. 2 and 3 is a flat plate structure, and a plurality of split-bubble micro holes are disposed on the plate surface. Fig. 2 shows an embodiment of a flat-plate single-side hinge obliquely-installed bubble structure 200, and fig. 3 shows an embodiment of a flat-plate straight-falling device bubble structure 200.

In specific implementation, the shape of the structure 200 shown in fig. 4 and 5 is a pyramid structure, where fig. 4 is an embodiment of the structure 200, and fig. 5 is an embodiment of the structure 200.

Specifically, the rupturing structure 200 is a rigid thin plate structure.

Specifically, the blister structure 200 is a mesh material structure.

In specific implementation, the net body material structure is in a tight state.

Specifically, the foam cracking structure 200 is disposed in the water storage body 100 in one or more of a horizontal arrangement, a single-side inclined arrangement, an opposite-side staggered inclined arrangement, a straight-falling arrangement, or a multiple-overlapping suspension arrangement.

In specific implementation, as shown in fig. 21, the crack structure 200 in the water storage 100 is horizontally arranged and is only suitable for purifying gas to be purified with no slag or very little slag.

Specifically, as shown in fig. 21 and 22, two side walls in the water storage body 100 are correspondingly provided with positioning structures 107 for horizontally placing the foam cracking structures 200 of the flat plate structure, specifically, the positioning structures 107 are horizontally fixed on the inner wall of the water storage body 100, and the positioning structures 107 of this embodiment are plate-shaped.

In specific implementation, as shown in fig. 1, the three-fold flat plate structure of the burst structure 200 in the water reservoir 100 is disposed with a single-side inclination.

In particular, as shown in fig. 6, the three-fold flat-plate structure of the burst bubble structure 200 in the water reservoir 100 is disposed in an inclined manner with the opposite sides staggered.

The flat-plate-shaped cracking and foaming structure 200 is obliquely arranged on one side and obliquely arranged on the opposite side in the water storage body 100 in a staggered manner, and is suitable for purifying waste gas containing slag, and waste slag generated after gas and slag separation is obliquely arranged and falls into the bottom of the water storage body 100 from a gap between the cracking and foaming structure 200 and the water storage body 100 for collection.

In specific implementation, as shown in fig. 7, the triple pyramid-shaped cracking structures 200 in the water storage body 100 are arranged in a superposed and suspended manner, and the pyramid-shaped cracking structures 200 can effectively and freely slide intercepted waste residues to sink to the bottom of the water storage body 100 for convenient collection.

In specific implementation, the straight-falling setting is that the inner side wall of the water storage body 100 is not provided with a fixed structure for placing the multiple foam cracking structure 200, and the foam cracking structure 200 is directly placed in the water storage body 100, namely, the straight-falling setting mode is adopted.

Preferably, a fixing structure for placing the multiple-cracking-foam structure 200 is arranged on the inner side wall of the water storage body 100, and the fixing structure is one or more of a single-side inclined slot, an opposite-side staggered inclined slot, a hanging rod tray, a step-shaped shelf strip or a smooth surface structure.

Specifically, the single-side inclined slot is that only one side wall in the water storage body 100 is provided with an inclined slot mounting strip 101 in a vertical strip shape, so that the foam cracking structures 200 of a plurality of flat plate structures are arranged in the notches 102 of the inclined slot mounting strip 101 in a single-side inclined manner, as shown in fig. 12, the inclined slot mounting strip 101 is provided with inclined notches 102; as shown in fig. 8 and 9, only one side wall of the water storage body 100 is provided with 3 inclined slot mounting bars 101, and the flat-plate structure of the bubble breaking structure 200 is obliquely hinged in the notches 102 of the inclined slot mounting bars 101.

Specifically, the opposite staggered inclined slots are two side walls in the water storage body 100 and are correspondingly provided with vertical strip-shaped inclined slot mounting strips 101, so that the foam cracking structures 200 of a plurality of flat plate structures are staggered in the notches 102 of the inclined slot mounting strips 101; as shown in fig. 10 and 11, two side walls of the water storage body 100 are correspondingly provided with 3 vertical strip-shaped inclined slot mounting bars 101, and the flat-plate structure of the cracking structure 200 is obliquely hinged in the notches 102 of the inclined slot mounting bars 101 in a staggered manner.

Specifically, as shown in fig. 13, hanging rod support platforms 103 for hanging multiple pyramid-shaped split foam assemblies are fixed on two sides of the inner side wall of the water storage body 100, fig. 14 is a schematic structural view of the multiple pyramid-shaped split foam assembly, and is formed by combining multiple pyramid-shaped split foam structures 200, hanging rods 104 and split foam plate stacking device rods 105, the multiple pyramid-shaped split foam assembly of the present embodiment is formed by stacking the triple pyramid-shaped split foam structures 200 on 2 split foam plate stacking device rods 105, fixing the triple pyramid-shaped split foam structures 200 on the tops of the 2 split foam plate stacking device rods 105 through one hanging rod 104, and placing the hanging rod 104 on the hanging rod support platforms 103, so that the multiple stacking suspension arrangement shown in fig. 7 can be achieved.

Specifically, as shown in fig. 15, 16 and 17, a plurality of steps are arranged on the two side walls in the water storage body 100, corresponding to the plurality of step-shaped shelf strips 106, and a plurality of steps are arranged in a stepped manner, so that the multiple flat-plate structure crack structure 200, the pyramid-shaped crack structure 200 or the bidirectional pyramid-shaped crack structure 200 can be sequentially placed on the steps, and are arranged in a manner of being narrow at the bottom and wide at the top, and are convenient to take;

in particular, fig. 18, 19, and 20 are embodiments in which the structure 200 of a plurality of bi-directional pyramids is placed on the stepped shelving strip 106.

Specifically, the smooth surface structure means that the inner side wall of the water storage body 100 is not provided with a fixing structure for placing the multiple cracked foam structure 200, and the cracked foam structure 200 is directly placed in the water storage body 100.

Specifically, the structural type of the water storage body 100 is one or a combination of civil engineering structural type, steel structural type and engineering plastic.

Specifically, a crack bubble purification chamber 110 is arranged in the water storage body 100, the crack bubble structure 200 is arranged in the crack bubble purification chamber 100, and the gas to be purified enters the crack bubble purification chamber 110 from the lower part of the crack bubble structure 200.

In specific implementation, the water storage body 100 is provided with the cracked foam purification chamber 110, the water storage body 100 of the embodiment is of a single-chamber structure, that is, the interior of the water storage body is the cracked foam purification chamber 110, the cracked foam structure 200 is arranged in the cracked foam purification chamber 100, and the gas to be purified enters the cracked foam purification chamber 110 from the lower part of the cracked foam structure 200.

Specifically, a gas introducing chamber 120 is further disposed in the water storage body 100, and the gas to be purified enters the cracking and foaming purifying chamber 110 through a gas guiding structure disposed in the gas introducing chamber 120.

In specific implementation, as shown in fig. 1, 6, 8, 10, 15 and 19, the water storage body 100 has a two-chamber structure, the water storage body 100 is further provided with a gas introducing chamber 120, the burst bubble purification chamber 110 and the gas introducing chamber 120 are separated by a baffle, as shown in fig. 1, the gas input interface 122 to be purified is provided on the outer side wall of the gas introducing chamber 120, the burst bubble purification chamber 110 is communicated with the lower part of the gas introducing chamber 120, and the gas to be purified enters the lower part of the burst bubble structure 200 in the burst bubble purification chamber 110 through the gas introducing structure via the lower part of the gas introducing chamber 120.

It should be noted that, if necessary, a plurality of functional chambers may be provided in the water storage body 100, that is, the water storage body 100 is provided with a multi-chamber structure, and all the adaptability adjustments made according to the inventive concept of the present invention belong to the embodiments of the present invention.

Specifically, the top of the water storage body 100 is in a uncovered mode, that is, the top is open, gas to be purified enters the lower part of the foam cracking structure 200 in the foam cracking purification chamber 110 from the lower part of the bleed air chamber 120, foam cracking or smashing and purification of liquid purification materials are carried out through the foam cracking structure 200 from bottom to top, and the purified gas is discharged from the upper part of the water storage body 100.

Preferably, a top cover 130 is further disposed above the water storage body 100, and an air outlet channel 131 is disposed on the top cover 130.

In specific implementation, the form of the top cover 130 can be set according to the communication condition of the bubble-splitting purification chamber 110 and the bleed air chamber 120 in the water storage body 100;

as shown in fig. 6-7, 10-11, 13, 15, 18, 19, 21, the upper air chambers of the burst bubble decontamination chamber 110 and the bleed air chamber 120 in the water reservoir 100 communicate with each other;

the top cover 130 shown in fig. 24-25 is selected, and the air outlet channel 131 of the top cover 130 is in communication with the cracked foam purification chamber 110 and the air introducing chamber 120, that is, the air outlet channel 131 is the air outlet channel 131 shared by the air introducing chamber 120 and the cracked foam purification chamber 110.

As shown in fig. 1, 8 and 9, the upper air chambers of the burst bubble clean room 110 and the bleed air room 120 in the water reservoir 100 do not communicate with each other; the top cover 130 shown in fig. 26-28 is selected, and the air outlet channel 131 is only communicated with the cracked foam purifying chamber 120.

It should be noted that the top cover 130 shown in fig. 26 to 28 is also applicable to the water storage body 100 of a single-chamber structure.

Specifically, as shown in fig. 1 and fig. 26 to 28, when the air chambers above the burst bubble purifying chamber 110 and the bleed air chamber 120 in the water reservoir 100 are not communicated with each other, the top cover 130 is provided with an air externally connecting passage 121 which establishes a separate communicating relationship with the bleed air chamber 120. The gas exhaust device is suitable for the gas to be purified which is high-temperature gas, such as boiler combustion waste gas, high-temperature steam can be generated in the gas introducing chamber 120, and the gas externally-connected channel 121 provides an output channel for the generated high-temperature steam, so that the steam is recycled, and resources are saved.

Preferably, a transverse gas guiding structure 140 is arranged in the bleed air chamber 120, so that the gas to be cleaned expands transversely in the direction of travel of the gas before entering the blister cleaning chamber.

Specifically, as shown in fig. 1 and fig. 6, a transverse air guide structure 140 communicated with the gas input interface 122 to be purified is disposed in the bleed air chamber 120, the transverse air guide structure 140 is used to transversely expand the gas to be purified that is about to enter the bubble splitting structure 200 disposed in the bubble splitting purification chamber 110, and the transverse air guide structure 140 promotes the transverse expansion of the gas to be purified along the gas traveling direction, so that the contact area between the bubbles after bubble splitting and the liquid purification material can be increased, and the purification effect can be improved.

In specific implementation, the transverse air guiding structure 140 shown in fig. 30-31 is provided with a single flat air outlet 141, that is, it is in a shape of a straight line, and the flat air outlet 141 is disposed below the cracked bubble structure 200, that is, below the joint of the air guiding chamber 120 and the cracked bubble purifying chamber 110 in the embodiment shown in fig. 1 and 6; through the structure of arranging the single flat air outlet 141, the gas to be purified is transversely unfolded, so that the gas to be purified occupies a wider range before the crack bubble purification, and a better crack bubble purification effect is obtained.

In specific implementation, the present invention further provides another transverse air guiding structure 140 as shown in fig. 32 and 33, wherein a plurality of parallel flat air outlets 141 are provided on the transverse air guiding structure 140, and the flat air outlets 141 are provided below the bubble splitting structure 200, that is, below the joint of the air guiding chamber 120 and the bubble splitting and purifying chamber 110 in the embodiment shown in fig. 1 and 6. Through the structure that sets up a plurality of flat mouth 141 of giving vent to anger side by side, make and wait to purify the gas and do horizontal expansion, for make before the crack bubble purifies wait to purify the gas and occupy wider range to obtain better crack bubble purification effect.

Specifically, as shown in fig. 32 and 33, a plurality of air flow dividing plates 142 corresponding to the flat air outlet 141 in the present embodiment are further disposed in the lateral air guide structure 140, and the air flow dividing plates 142 have the function of further dispersing the air flow.

Preferably, the longitudinal gas guide structure 150 is disposed above the flat gas outlet 141 of the transverse gas guide structure and below the bubble splitting structure 200, so that the gas to be purified after transverse expansion longitudinally expands in the gas traveling direction before entering the bubble splitting structure 200.

In specific implementation, the longitudinal air guide structure 150 shown in fig. 34 to 37 is a groove structure, a plurality of longitudinal air flow dividing pieces 151 are obliquely arranged on the longitudinal air guide structure 150 in parallel, and an air outlet 152 is formed between two adjacent longitudinal air flow dividing pieces 151.

Preferably, the longitudinal air flow dividing pieces 151 are arranged in different gradients.

Specifically, the length of the longitudinal gas flow dividing pieces 151 is sequentially increased in the gas traveling direction.

The longitudinal expansion principle is as follows: the air flow output from the plurality of parallel flat air outlet ports 141 of the transverse air guide structure 140 is restrained in the groove due to the buoyancy thereof, and the longitudinal air flow dividing pieces 151 in the echelon layout longitudinally spread the air flow into a plurality of strands of floating air flow.

The gas to be purified which is expanded transversely is longitudinally expanded by matching with the plurality of parallel flat gas outlet ports 141 of the transverse gas guide structure 140 in fig. 32, so that the gas to be purified occupies a wider range before the crack bubble purification, and a better crack purification effect is obtained.

As shown in fig. 38-40, the present invention also provides another longitudinal gas directing structure 150,

specifically, the longitudinal air guide structure 150 is shaped like a groove, and a plurality of air outlets 152 are distributed on a panel of the groove and are in a mesh shape.

The longitudinal expansion principle is as follows: the air flow output from the plurality of parallel flat air outlet ports 141 of the transverse air guide structure 140 is restrained in the groove due to the buoyancy thereof, and the plurality of air outlet ports 152 arranged on the panel of the groove longitudinally spread the air flow into a plurality of strands of floating air flow.

The gas to be purified which is expanded transversely is longitudinally expanded by matching with the plurality of parallel flat gas outlet ports 141 of the transverse gas guide structure 140 in fig. 32, so that the gas to be purified occupies a wider range before the crack bubble purification, and a better crack purification effect is obtained.

The invention relates to a gas cracking and foaming purification system, which adopts the gas cracking and foaming purification device as shown in any one of the above 1-23, and further comprises a gas introducing device and an exhaust device, wherein the gas introducing device is used for conveying gas to be purified into the gas cracking and foaming purification device, and the exhaust device is used for exhausting the purified gas from the gas cracking and foaming purification device.

In specific implementation, the operation mode of the inducing device may be that an induced draft fan is arranged at the front end of the gas transmission channel to forcibly input the gas to be purified into the water storage 100, or the water storage 100 is set to be negative pressure, and the gas to be purified is sucked into the water storage 100, or the two are combined to form a double-introducing mode.

In specific implementation, the operation mode of the exhaust device may specifically be: the low-altitude air exhaust system comprises a low-altitude air exhaust channel, a high-altitude air exhaust channel, a draught fan, an output channel and a draught fan, wherein the low-altitude air exhaust channel is used for naturally exhausting low altitude air, the high altitude air exhaust channel is used for forcibly exhausting the low altitude air, and the high altitude air exhaust channel is used for forcibly exhausting the high altitude air through the output channel and the draught fan.

Preferably, the system further comprises a slag discharging device, wherein the slag discharging device comprises a slag collecting structure arranged at the bottom of the water storage body 100, a mechanical inner slag discharging mechanism is arranged in the slag collecting structure, and the mechanical inner slag discharging mechanism is used for discharging the sediment in the slag collecting structure from the inside of the water storage body.

In specific implementation, as shown in fig. 1, 6, 7 and 41, a cone-hopper-shaped slag collection structure 160 is provided at the bottom of the water storage body 100, an internal mechanical slag discharge mechanism 161 is provided in the slag collection structure 160, and the internal mechanical slag discharge mechanism 161 is used for discharging the sediment in the slag collection structure 160 from the inside of the water storage body 100. The slag discharging device is suitable for slag-containing gas to be purified, and is convenient for collecting and discharging waste slag.

Specifically, the mechanical internal slag discharging mechanism 161 is one or a combination of several of a screw, a chain scraper, a chain bucket, and a conveyor belt.

Preferably, the device further comprises a mechanical material conveying device 162 matched with the mechanical internal slag discharging mechanism 161, wherein the mechanical material conveying device 162 is used for remotely transferring the sediments discharged by the mechanical internal slag discharging mechanism.

As shown in fig. 41, the mechanical material conveying device 162 is disposed outside the water storage body 100, and is disposed in an inclined manner, and the stack is transferred by lifting the stack height, specifically, the mechanical material conveying device 162 is one or a combination of several of a spiral, a chain scraper, a chain bucket, and a conveyor belt.

It should be noted that the mechanical material conveying device 162 and the mechanical internal slag discharging mechanism 161 may be driven by independent belts or by a transmission device sharing the same power source.

Preferably, the water storage body further comprises a water replenishing device, wherein the water replenishing device comprises a water replenishing pipe, and the water replenishing pipe is communicated with the inside of the water storage body.

In specific implementation, as shown in fig. 21, the water replenishing device includes a water replenishing pipe 170, and the water replenishing pipe 170 is communicated with the inside of the water storage body 100.

Specifically, as shown in fig. 21, a drain device including a drain pipe 180 disposed at the bottom of the water storage body 100 is further included.

In particular, as shown in the drawings, the bottom of the water reservoir 100 is provided with a drain 180 for draining the liquid purification material in the water reservoir 100, and the water reservoir 100 provided with the drain 180 is generally in the form of a flat bottom.

Preferably, the scum discharging and collecting device is further included.

In particular, the scum discharging and collecting device is disposed in the water storage 100 for separating water from oil scum/scum and collecting and discharging the oil scum/scum, which can be one or more of a combination of circulating moving scrapers, a blowing scum discharging device or a water spraying scum discharging device.

Preferably, an auxiliary agent adding device is further included.

Preferably, the device also comprises a sampling inspection device for inspecting the purified water and gas as an inspection object, and the sampling inspection device is used for inspecting the purification quality/effect of the purified gas; checking the pollutant content in the purified water, and the like.

Preferably, the system also comprises a control and operation system, so that remote monitoring is facilitated, and the safety performance is improved.

Preferably, a purified gas optimizing device is further included.

Preferably, the system also comprises a system for recycling the waste water and the waste residue after gas purification.

The quick-boiling type bulb splitting purification and the structure that the post-stage water replenishing is towards the pre-stage are implemented, so that the purification substances contained in the first-stage purified water are high in concentration, the purification substances are led out for centralized processing, and the useful substances contained in the first-stage purified water are extracted, so that the efficiency and the value are high.

It should be noted that the slag discharge device, the froth discharge and collection device, the auxiliary agent addition device, the sampling inspection device for inspecting the purified water and gas, the control and operation system, the purified gas optimization device, and the gas purified wastewater and waste residue recycling system are systems/devices that can be selectively implemented and set according to the performance of the gas to be purified and the purification requirements.

The invention also provides a cascade gas cracking and foaming purification system, which is formed by connecting a plurality of gas cracking and foaming purification systems randomly arranged in series.

In specific implementation, the purification stages of the cascaded cracking foam purification system are at least two stages, namely at least two gas cracking foam purification systems are arranged in series through a pipeline;

as shown in fig. 42-43, the present invention provides an embodiment of a cascaded cracking bubble scrubbing system with three stages of scrubbing:

the gas to be purified treated by the first-stage gas purification device has more slag content, and the water storage body 100 is generally provided with a slag discharging device, namely, the bottom of the water storage body is provided with a slag collecting structure 160 and a mechanical internal slag discharging mechanism 161 to implement continuous slag discharging, so that gas and slag separation is facilitated, and primary purification of gas is achieved;

the slag content of the gas to be purified treated by the secondary gas purification device is less, the bottom of the water storage body 100 is generally provided with a slag collecting structure 160, but the slag is not required to be discharged through a mechanical internal slag discharging mechanism 161, only a pumping slag discharging interface 163 is arranged on the side surface of the water storage body 100 close to the bottom, and the gas and a small amount of waste slag are separated conveniently by continuously discharging slag through a simple pumping slag discharging mode; further purification of the gas is achieved;

the gas to be purified treated by the final-stage gas purification device is basically free of slag and does not need to be discharged, so that the bottom of the water storage body 100 is generally of a flat bottom structure, and the bottom is provided with a drain pipe 180 for draining water, so that deep purification of the gas is realized, and high-quality purified gas is obtained.

The cascaded gas cracking bubble purification system is characterized in that the gas to be purified is introduced into the front end of the cracking bubble structure in a quick boiling mode, the whole gas to be purified is subjected to water bath purification of liquid purification materials, the phenomenon that part of the gas to be purified is not purified is hardly generated, and if the cascaded purification is combined, the condition of the later-stage purification, such as targeted additive injection of a purification facility aiming at specific substances contained in the gas to be purified, supports different purification targets, and has ultrahigh purification efficiency.

According to the cascade gas cracking bubble purification system provided by the invention, each cascade purification unit also allows different purification materials to be used to achieve different purification targets, for example, the first-stage main purification target is in dust removal; the second stage of primary purification targets desulfurization; the third stage mainly aims at denitration; the fourth stage of purification aims at the purification of special harmful substances contained in special gas and the like.

Further, when the cascaded gas cracking and foaming purification system provided by the invention is applied to purification treatment of different types of gases, the composition, function target, operation flow and the like of the cascaded gas cracking and foaming purification system can be different, such as purification treatment of toxic and harmful gases, purification treatment of odor, purification treatment of biochemical gases, pure air purification and fresh air supply systems and the like.

The invention also provides a cluster type gas cracking bubble purification system which is formed by connecting a plurality of cascaded gas cracking bubble purification systems in parallel.

When the system is specifically implemented, a plurality of cascaded gas cracking and bubble purifying systems are deployed in parallel to form a cluster type gas cracking and bubble purifying system, so that the deep purification treatment requirement of large or ultra-large industrial waste gas can be met.

FIG. 45 shows an embodiment of a clustered gas cracking system composed of three cascaded cracking systems with three purification stages in parallel.

Specifically, as shown in fig. 46-49, the cluster-type gas cracking and bubbling cleaning system of this embodiment further includes a gas input distribution valve 190 for the gas to be cleaned, the gas input distribution valve 190 has a main input port 191 at one end and a plurality of branch gas transmission ports 192 at the other end, and the branch gas transmission ports are connected to the gas cleaning device through pipes. Any one set of cascaded purge systems is arranged to be in a standby state by the deployment of purge gas input distribution valves 190 to support emergency needs and facilitate duty-off maintenance.

Preferably, as shown in fig. 42 to 43, adjacent gas purification devices are communicated with each other through an interstage water replenishing pipe 171 to form a water replenishing pattern from back to front, and specifically, one end of the interstage water replenishing pipe 171 is located at a high level of the water storage body 100 of the preceding-stage gas purification device, and the other end is located at a low level of the water storage body 100 of the following-stage gas purification device; the final gas purification device is directly replenished with water through a water replenishing pipe 170. Because the water in the gas purification device at the final stage is cleaner, the water purification device can be used by the previous gas purification device, the utilization rate of the water in the gas purification device at the final stage is improved, and water resources are saved.

The invention also provides a gas cracking bubble purification method, which comprises the following steps:

the method comprises the following steps: deploying a gas purification apparatus as described in any of the above;

a second step of introducing the gas to be purified into the front end of the bulb splitting structure 200 arranged in the water storage body 100 in a quick-boiling manner;

step three: the gas to be purified which is introduced into the water reservoir 100 is subjected to at least one of the breaking or fragmentation of the breaking structure 200 and is purified by the liquid purification material;

step four: the purified gas is discharged from the water storage body 100.

In specific implementation, the gas to be purified is subjected to the breaking or fragmentation of the breaking structures and the purification of the liquid purification material by introducing the gas to be purified in a quick-boil manner to the front ends of the breaking structures 200; meaning that the whole of the gas to be purified is subjected to the water bath purification of the liquid purification material, there is hardly any phenomenon that a part of the gas to be purified is not purified, and thus the purification efficiency is ultra-high.

The area, depth, and form of the water reservoir 100 can be determined according to the nature, load, and purification requirements of the gas to be purified, installation environment, and the like, to thereby achieve bubble-breaking purification of the gas.

Preferably, the gas subjected to cracking foam purification on the gas to be purified without waste slag is directly discharged from the water storage body 100; the gas and slag separation is realized while the gas to be purified containing the waste slag is purified by cracking bubbles, the purified gas is discharged from the water storage body 100, and the waste slag generated in the period automatically deposits and gathers at the bottom of the water storage body 100 and is transferred out of the water storage body 100 through a slag discharge device.

Preferably, the method further comprises the following step five: the purified waste water/waste residue is transferred, processed and utilized, thereby realizing the reutilization of the waste water/waste residue, saving resources and being beneficial to environmental protection. The waste water/waste residue recycling principle is as follows: through quick-boiling formula crack bubble purification and back level towards preceding stage moisturizing structure for the purifying substance concentration that contains is big in the first grade of purification aquatic, exports it and carries out centralized processing, extracts the useful substance that contains wherein, so efficiency and value are high.

Preferably, the deployment of gas cleaning devices is arranged in series by a plurality of gas cleaning devices to form a cascaded gas bubble cleaning system.

In specific implementation, the purification stages of the cascaded cracking foam purification system are at least two stages, namely at least two gas cracking foam purification systems are arranged in series through a pipeline, so that the gradual purification is realized, and the purification effect is improved;

preferably, the deployment of gas cleaning devices is arranged in parallel by a plurality of said cascaded gas cracking cleaning systems to form a clustered gas cracking cleaning system.

When the system is specifically implemented, a plurality of cascaded gas cracking and bubble purifying systems are deployed in parallel to form a cluster type gas cracking and bubble purifying system, so that the deep purification treatment requirement of large or ultra-large industrial waste gas can be met. Meanwhile, any group of cascade purification systems are arranged to be in a standby state through the allocation of the gas to be purified input distribution valve 190 so as to support the requirement of sudden working conditions and facilitate the maintenance of wheel value.

Preferably, adjacent gas purification apparatuses are sequentially communicated with each other through the interstage water replenishing pipe 171 to form a back-to-front stage water replenishing mode, and the gas purification apparatus at the final stage is directly replenished with water through communication with the water replenishing pipe 170.

In specific implementation, as shown in fig. 42 to 43, the adjacent gas purification devices are communicated with each other through the interstage water replenishing pipe 171 to form a water replenishing mode from back to front, so that the utilization rate of water in the final-stage gas purification device is improved, and water resources are saved.

The invention also provides an application of the gas cracking bubble purification method.

The invention can apply the gas cracking bubble purifying method as described above to other gas purifying fields, such as purifying gaseous pollutants generated in industrial production process, purifying environmental gas and purifying gas for other purposes, by means of cracking and bursting, when gas enters into the cracking structure, the bubble diameter of the purified gas bubbles passing through the purified water is compressed as much as possible (the purified gas bubbles can be dispersed in multiple steps), the gas wrapped in the bubbles is fully released, the contact surface area and contact opportunity of the purified gas bubbles and the purified water are promoted, the traveling route of the bubbles is designed in the purified water body, the path length of the purified gas bubbles passing through the purified water is prolonged as much as possible, and the effect of the purified water on the purified gas is strengthened as much as possible (including the expansion change of the additive for strengthening the purifying effect on the purified water), thereby surpassing the purification effect of the traditional wet purification method on the gaseous mixture.

The method is particularly applied to the following fields: the method comprises the following steps of boiler flue gas purification, industrial smoke (smoke produced in the industrial production process), industrial pure dust (dust produced in the industrial production process) purification (including pure precipitated dust, pure floating dust, mixed dust of both precipitated dust and floating dust), oil-containing flue gas purification, odor purification (typical toilet odor purification), poisonous and harmful gas purification, air sterilization and purification in closed epidemic areas (quick-boiling type pathogen sterilization and purification in self-circulating air of infectious disease areas), maintenance of clean air in closed equipment or (combat readiness) engineering, preparation of clean air in ultra-clean environment, air purification of a fresh air supply system, recovery of useful substances in smoke and gas and other related fields of gas purification, wherein the smoke purification flow given according to the cigarette gas purification method can be adopted as the basic flow of other gas purification, according to different specific flue gas purification objects, different purification purposes, different purification conditions and the like, corresponding changes are made on the basis of the flow, so that the requirements of purifying most other different gases can be met, and a more effective flue gas purification effect is realized.

In particular, it can also be used for producing some gas purification machines, such as the production process field gas water bubbling purifier type; the gas water cracking purifier is used for the public environment such as residence, office, business, transportation and the like; a toxic gas water cracking and foaming purifier type; odor water cracking purifier type; a purifying machine type for preventing biochemical attack on air water from cracking and foaming; water crack bubble purifies send new trend system.

The invention also provides a household cracking foam method air purifier adopting the gas purification device, wherein an outer air inlet 301 is arranged at the outer side of the water storage body 100, an inner induced air outlet 302 is arranged below the cracking foam structure 200, the outer air inlet 301 is communicated with the inner induced air outlet 302 through a built-in induced air duct 303, a fan 304 is installed at an upper opening of the water storage body 100, and an air outlet of the fan 304 is arranged outwards.

In specific implementation, as shown in fig. 50 to 53, the water storage body 100 has a cylindrical shape, and the water storage body 100 is provided therein with a burst bubble structure 200 and a liquid purification material such as water or modified water. An outer air inlet 301 is arranged around the outer side of the water storage body 100, an inner air outlet 302 is arranged below the bubble cracking structure 200, the outer air inlet 301 is communicated with the inner air outlet 302 through a built-in air guide channel 303, a fan 304 is installed at an upper opening of the water storage body 100, the fan 304 can generate negative pressure, an air outlet of the fan is arranged outwards, gas to be purified enters from the outer air inlet 301, enters the bottom of the water storage body 100 through the built-in air guide channel 303 and the inner air outlet 302, and is subjected to bubble cracking or smashing through the bubble cracking structure 200 and purification of liquid purification materials and then is discharged from the air outlet.

Preferably, a drain hole is disposed in the bottom of the water storage body 100, and the drain hole is provided with a water plug 305.

In specific implementation, as shown in fig. 52, a drain hole is disposed at the bottom of the water storage body 100, and a water plug 305 is disposed at the drain hole to facilitate manual drainage.

Preferably, the burst structure 200 is a multiple cone burst structure.

In specific implementation, as shown in fig. 50, the split-bubble structure 200 is a multiple cone-shaped split-bubble structure, so as to improve the gas purification effect.

Preferably, the air outlet of the fan 304 is provided with a radial outlet 306 for purified air.

In specific implementation, as shown in fig. 50 to 53, the air outlet device of the fan 304 has a radial outlet 306 for discharging air, and the radial outlet 306 is set to discharge air radially, so as to prevent dust or foreign matters from falling into the outlet 306 from the top of the device and causing blockage.

The invention also provides a gas table type cracking bubble purifier adopting the gas purifying device, wherein a circumferential air channel 402 communicated with an induced air pipe 401 is arranged below the water storage body 100, an air outlet leading to the interior of the water storage body 100 is formed in the circumferential air channel 402, and the air outlet is arranged at the bottom or near the bottom of the cracking bubble structure 200; the upper opening of the water storage body 100 is further provided with a cover 403, the cover 403 is provided with a fan 304, and an air outlet of the fan 304 is arranged outwards.

In specific implementation, as shown in fig. 54-57, the water storage body 100 has a barrel-shaped conical bottom, and the water storage body 100 is provided therein with a multi-cone-shaped cracking-foam structure 200 and a liquid purification material such as water or modified water. A circumferential air duct 402 communicated with an air guide pipe 401 is arranged below the water storage body 100, a plurality of air outlets leading to the interior of the water storage body 100 are formed in the circumferential air duct 402, and the air outlets are arranged at the bottom or near the bottom of the cracking bubble structure 200; the upper opening of the water storage body 100 is further provided with a cover 403, the cover 403 is provided with a fan 304, and an air outlet of the fan 304 is arranged outwards. The gas to be purified enters from the induced draft tube 401, enters the bottom of the water storage body 100 through the air outlet on the circumferential air channel 402, is cracked or crushed through the cracking structure 200, is purified by the liquid purification material, and is discharged from the air outlet of the fan 304.

Preferably, the upper portion of the water storage body 100 is provided with a fastening device which is matched with the cover 403, so that the cover 403 and the opening of the water storage body 100 can be conveniently opened and hermetically fastened.

During specific implementation, the upper part of the water storage body 100 is provided with a fixed connection fastener matched with the cover body 403, so that the cover body 403 and the water storage body 100 are conveniently and hermetically connected and conveniently opened.

Preferably, the side of the water storage body 100 is further provided with an injection port 404 for water/additive, and the bottom of the water storage body 100 is further provided with a discharge port 405 for water/sediment.

In specific implementation, as shown in fig. 54-57, the side of the water storage body 100 is further provided with an injection port 404 for water/additive, and the bottom of the water storage body 100 is further provided with a discharge port 405 for water/sediment, so as to facilitate the operations of adding water/additive and draining/deslagging to the equipment.

Although terms such as water reservoirs, inclined slot mounting bars, cracked foam slab stacking device bars, cracked foam structures, stepped shelving bars, mechanical internal deslagging mechanisms, mechanical material delivery devices, pumping deslagging interfaces, gas to be purified input distribution valves, longitudinal gas flow dividing sheets, gas to be purified input interfaces, hanging bar pallets, cracked foam purification chambers, gas external channels, etc., are used more often herein, the possibility of using other terms is not excluded. These terms are used merely to more conveniently describe and explain the nature of the present invention; they are to be construed as being without limitation to any additional limitations that may be imposed by the spirit of the present invention.

Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the invention has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.