CN104128059B - Percussion flow gas purge system - Google Patents
Percussion flow gas purge system Download PDFInfo
- Publication number
- CN104128059B CN104128059B CN201410366353.3A CN201410366353A CN104128059B CN 104128059 B CN104128059 B CN 104128059B CN 201410366353 A CN201410366353 A CN 201410366353A CN 104128059 B CN104128059 B CN 104128059B
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- reaction room
- flow type
- clean unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Abstract
The invention discloses a kind of percussion flow gas purge system, comprise the clean unit device that several orders are arranged separately, by the first pipeline communication between adjacent two clean unit devices; Each clean unit device comprise upright shock flow type gas-liquid reaction room, handstand shock flow type gas-liquid reaction room and be communicated with the second tube connector; Convoluted liquid jet pipe is deep into positive flow passage and the reverse flow passage of shock flow type gas-liquid reaction indoor; Ultraviolet lamp is provided with in the first pipeline being communicated with adjacent two clean unit devices; The end of the shock flow type gas-liquid reaction room of the handstand of each clean unit device is also provided with auto purification type catalytic membrane; Auto purification type catalytic membrane comprises stainless (steel) wire and is plated in the titanium dioxide layer on stainless (steel) wire; The clean unit device being positioned at least significant end is provided with gas-liquid separation chamber successively; Gas-liquid separation indoor are provided with gas-liquid separation guide plate and gas-liquid separation membrane.This system can carry out high efficiency purified treatment to the air scale of construction and containing the gas of Multiple components.
Description
Technical field
The present invention relates to air cleaning facility field, particularly relate to a kind of percussion flow gas purge system.
Background technology
Present urban air-quality worse and worse, people are also more and more stronger to the demand improving air quality, people are for pm2.5 (particulatematter, particle), namely in surrounding air, aerodynamics equivalent diameter is less than or equal to the particle of 2.5 μm (microns), also claims fine particle.This numerical value of pm2.5 is higher, and just to represent air pollution more serious.But in daily industrial production, the gas usually discharging a large amount of heterogeneity causes (comprising the solid particle, dust, organic pollutant etc. that pollute class) pollution of air;
Air purifier carries out classification by cleaning principle three kinds:
1, absorbent-type is filtered: utilize porous filter material, as (the strongest the working as of current adsorption capacity count HEPA high-density air filter material) such as non-woven fabrics, filter paper, fiber, foam cottons, suspended particulate in absorbed air, pernicious gas, thus purify air.2, electrostatic precipitation type: make pollutants in air charged by electrostatic, has then adsorbed the dirt in air of charged particle with dust collect plant trapping, has reached the object that purifies air.3, compound: to utilize filtration and electrostatic precipitation mode to purify air simultaneously.
Wherein: filter absorbent-type, such as: (1) adopts and considers material, consider plate, filter cylinders etc. have (it are comparatively obvious for particle rich) such as type gas film or active carbons, but it is of long duration, the film body of gas film is bound to the Particulate Pollution after by enrichment, thus the air after its process causes secondary pollution, and the film body of this gas film is non-renewable (because the particle of its attachment is often very little, composition is very complicated, but the gas film after cleaning equally also adheres to such particle, cannot continue to use), what is more important its to the air scale of construction and multicomponent gas cleaning more aobvious helpless.
Wherein, its process gaseous substance of electrostatic gas purifying equipment is very single, can not effectively be removed VOC.
Wherein, in compound gas purifying equipment, the main filtrate that adopts is prepared filter screen or filter cylinder and carries out enrichment in conjunction with electrostatic apparatus to the particle in air; Or (VOC material refers to the general name holding volatile organic substance at normal temperatures, common are formaldehyde, toluene and dimethylbenzene etc. to the VOC gas that contains of little a part of little gas flow to adopt some polar substances (such as: sulphur fiber leaching some chemical substance profound).) carry out degrading and removing; But still there is the technological deficiency of following several aspect in it: when gas film and electrostatic depuration structure composite use, windage is larger, it can not carry out high efficiency purification to the gas of the air scale of construction, treating capacity is very little, still there is a large amount of polluter in air can not be purified, its purified treatment efficiency is very low.Its process gas componant is also few; The middle sulfur dioxide of such as coal-fired air cannot be removed.
In the prior art as immediate technical scheme, relate to a kind of household kitchen oil smoke cleaning equipment (namely number of patent application is 03102035.6), its primary structure comprises anterior shock flow type gas-liquid reaction room 2 and the gas-liquid separation chamber at rear portion, wherein; The shock flow type gas-liquid reaction room 2 of upright placement comprises air inlet 21 and deflector I (i.e. the first deflector 23), bilateral symmetry is provided with deflector II (i.e. the second deflector 25), middle part forms air impingement district (chamber 24 of namely clashing), is impingement region outlet (i.e. exhaust outlet 22) bottom it; At least one pair of jet pipe is set in the space in this air impingement district; This is arranged in same plane in opposite directions to the spray-hole of jet pipe; The flange at the two ends of the first deflector 23 forms positive flow passage 26 and reverse flow passage 27 with the second deflector 25 of below respectively.Gas-liquid separation chamber, its top arranges a pair deflector III, form both sides gas discharge outlet, and form gas collection district at top, the middle part in this gas collection district is provided with outlet, this technical scheme has following characteristics, this solution provides a kind of high speed, initiatively, gas-liquid reactor, can be separated and enrichment with to trace constituent different in gas carrying out the higher reaction of efficiency compared with the air scale of construction within a short period of time.The program has following deficiency: 1. only carried out a gas-liquid contact to pending gas, can not carry out the gas-liquid contact of the degree of depth and Duo Bo time.2. a kind of liquid can only be adopted as gas-liquid contact media, reaction and separation processes enrichment process can not be carried out to the gas containing multiple heterogeneity.3. this technical scheme can not form efficiency light catalyst structure, thus very low to efficiency when carrying out chemical reaction containing the gas of different chemical composition.
Summary of the invention
The object of the present invention is to provide a kind of percussion flow gas purge system, to solve the problem.
In order to achieve the above object, technical scheme of the present invention is achieved in that
The invention provides a kind of percussion flow gas purge system, comprise the clean unit device that several orders are arranged separately, by the first pipeline communication between adjacent two described clean unit devices; Each described clean unit device comprise upright shock flow type gas-liquid reaction room, handstand shock flow type gas-liquid reaction room and be communicated with second tube connector of shock flow type gas-liquid reaction room of upright shock flow type gas-liquid reaction room, handstand; Described second tube connector is turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction room, the shock flow type gas-liquid reaction room of handstand are relative to the second symmetrical setting in tube connector left and right;
Also comprise liquid supply conduit, liquid backflow pipeline and the liquid case for splendid attire polytype reactant liquor; And be also provided with the pump housing in described liquid case;
One end of described liquid supply conduit is communicated with the pump housing of described liquid case inside, and the other end is provided with convoluted liquid jet pipe capable of circulation, and is deep into positive flow passage and the reverse flow passage of shock flow type gas-liquid reaction indoor; One end of described liquid backflow pipeline is communicated with the bottom of described second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
Also ultraviolet lamp is provided with in the first pipeline between adjacent two the described clean unit devices of each connection;
The end of the shock flow type gas-liquid reaction room of the handstand of each described clean unit device is also provided with auto purification type catalytic membrane; Described auto purification type catalytic membrane comprises stainless (steel) wire and is plated in the titanium dioxide layer on described stainless (steel) wire;
The clean unit device being positioned at least significant end is also provided with gas-liquid separation chamber successively; Described gas-liquid separation indoor are provided with gas-liquid separation guide plate and gas-liquid separation membrane.
Preferably, modularization magnetic purifier is equipped with in positive flow passage described in described shock flow type gas-liquid reaction room and described reverse flow passage; Described modularization magnetic purifier comprises the permanent magnet of many group arranged opposite distribution; Described convoluted liquid jet tube portion is through many group permanent magnets; Described convoluted liquid jet pipe is provided with the spray hole in line segment shape that multiple length direction along pipe is offered.
Compared with prior art, the advantage of the embodiment of the present invention is:
Analyze above-mentioned air purification structure known: the main modified node method of above-mentioned percussion flow gas purge system is:
1, several clean unit devices sequentially arranged separately, the top (or top) between adjacent two described clean unit devices by the first pipeline communication, thus forms continuous print multistage purification equipment;
2, each described clean unit device comprise upright shock flow type gas-liquid reaction room, handstand shock flow type gas-liquid reaction room and be communicated with second tube connector of shock flow type gas-liquid reaction room of upright shock flow type gas-liquid reaction room, handstand; Described second tube connector is turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction room, the shock flow type gas-liquid reaction room of handstand are relative to the second symmetrical setting in tube connector left and right;
Wherein, each clean unit device has following structure: its left end is handstand gas-liquid separation chamber by upright gas-liquid separation chamber, its right-hand member, middle to connect and compose by turning through 180 degree second tube connector at angle, the symmetrical setting in left and right, shock flow type gas-liquid reaction room of upright shock flow type gas-liquid reaction room, handstand.
3, also ultraviolet lamp is provided with in the first pipeline between adjacent two the described clean unit devices of each connection; The end of the shock flow type gas-liquid reaction room of the handstand of each described clean unit device is also provided with auto purification type catalytic membrane; Described auto purification type catalytic membrane comprises stainless (steel) wire and is plated in the titanium dioxide layer on described stainless (steel) wire.Above-mentioned titanium dioxide is as catalyst, under the irradiation of ultraviolet lamp, catalytic membrane surface can form light induced electron and this photocatalyst structure of photohole to be had stronger oxidation and reducing power and can carry out Strong oxdiative and reduction reaction to VOC (namely mainly organic matter volatile matter), is small-molecule substance (such as carbon dioxide and water) after above-mentioned reaction by the Molecular Cloning greatly of VOC; And produce a large amount of negative oxygen ions.It should be noted that, ultraviolet lamp set in the first pipeline and the catalytic membrane set by last reactor end are a kind of photocatalyst structure necessary conditions each other.This structure can be degraded toxic and harmful in air effectively; Effectively can kill various bacteria, and the toxin that bacterium or fungi can be discharged decomposes and harmless treatment, the function such as simultaneously also possess deodorizing, anti-soil, purify air.A large amount of negative oxygen ions can optimize air quality, provides the air ambient of a high-quality.
4, liquid supply conduit, liquid backflow pipeline and the liquid case for splendid attire polytype reactant liquor is also comprised; And be also provided with the pump housing in described liquid case; One end of described liquid supply conduit is communicated with the pump housing of described liquid case inside, and the other end is provided with convoluted liquid jet pipe capable of circulation, and is deep into positive flow passage and the reverse flow passage of shock flow type gas-liquid reaction indoor; One end of described liquid backflow pipeline is communicated with the bottom of described second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
Modularization magnetic purifier is equipped with in positive flow passage described in described shock flow type gas-liquid reaction room and described reverse flow passage; Described modularization magnetic purifier comprises the permanent magnet of many group arranged opposite distribution; Described convoluted liquid jet tube portion is through many group permanent magnets; Described convoluted liquid jet pipe is provided with the spray hole in line segment shape that multiple length direction along pipe is offered.
In said process, when gas enters shock flow type gas-liquid reaction room, one end and the liquid case of liquid supply conduit (it comprises polytype solution, such as Ozone Water, filtered water, reactant liquor etc.) the inner pump housing is communicated with, the other end is provided with convoluted liquid jet pipe capable of circulation, and is deep into positive flow passage and the reverse flow passage of shock flow type gas-liquid reaction indoor; Above-mentioned gas can implement fluid purification operation in the positive flow passage of shock flow type gas-liquid reaction indoor and reverse flow passage;
The gas of discharging from the impingement region outlet of upright shock flow type gas-liquid reaction room is first lowered through the bottom of the second tube connector, then the gas that (this process have passed through turn through 180 degree angle place) enter rapidly the shock flow type gas-liquid reaction room of handstand that rises enters mouth, completes rapidly the purified treatment flow process of a purifying treating unit; Gas enters the purifying treating unit of next stage by the first pipeline subsequently.
5, modularization magnetic purifier is equipped with in positive flow passage described in shock flow type gas-liquid reaction room and reverse flow passage.
The operation principle analyzing above-mentioned percussion flow gas purge system is known: the gas containing Various Complex chemical composition (being rich in the compositions such as various particulate matter, VOC or SO2) first enters pre-treatment purifier at a high speed under the effect of blower fan, and pre-treatment purifier carries out enrichment, sedimentation to particulate matter in percussion flow gas liquid reaction indoor by oxygen rich gas and high-temperature steam; Then pending gas enter immediately in several clean unit devices of continuous print carry out many ripples time, the gas purification of high-speed and continuous; When entering each clean unit device, all successively enter the modularization magnetic purifier of upright shock flow type gas-liquid reaction room and inside and the shock flow type gas-liquid reaction room of the second tube connector and handstand; And carry out being oxidized and reduction reaction on catalytic membrane surface under the irradiation of ultraviolet lamp by catalytic membrane.Concrete condition: after the gas that gas to be clean enters upright shock flow type gas-liquid reaction room enters mouth, first run into first deflector with the protruding globoidal structure in middle part that housing central section is provided with, then promptly to along the first deflector two ends flowing, positive flow passage and reverse flow passage is entered subsequently; In positive flow passage and reverse flow passage after magnetic purifying process, enter air impingement district; Gas-liquid mixture in air impingement district is movement velocity fast (namely ensureing that in air scale of construction gas, trace constituent carries out high speed enrichment) not only, and can realize high speed purifying and sedimentation for the dusty gas of heterogeneity and particle; In addition, the impingement region outlet of upright shock flow type gas-liquid reaction room is arranged downwards; Gas is discharged to decline from impingement region outlet rapidly and is entered the bottom of the second tube connector and the second tube connector, and quick rising of turning enters the shock flow type gas-liquid reaction room (simultaneously completing knock-on reaction) of handstand subsequently;
Wherein: modularization magnetic purifier is when magnetic purifying process, in positive flow passage and reverse flow passage, convoluted liquid jet pipe jetting liquid (such as: Ozone Water or reactant liquor, these liquid sprayed will carry out purified treatment to air), and in liquid, often there is charged particle and ion) be subject to the effect of the Lorentz force of magnet assemblies (i.e. the concrete structure of modularization magnetic purifier) under, particle enrichment region is formed rapidly at positive flow passage and the motion of reverse flow passage interior orientation, this enrichment region and impingement region overlap, enhance reaction rate and the rate of settling.The gas high-speed impact of positive flow passage and reverse flow passage, forms the exclusive concussion process of percussion flow, makes partially liq molecular polarization and enhances enrichment and the infall process of chemical reaction process and particle.
Due on same level direction, constitute multistage purification equipment by multiple clean unit device separately; So air to be clean all successively can enter upright shock flow type gas-liquid reaction room, modularization magnetic purifier and the second tube connector after entering first class purification cell arrangement at every turn, the shock flow type gas-liquid reaction room of handstand, modularization magnetic purifier; With the photocatalyst structure be made up of catalytic membrane and ultraviolet lamp.Due to the distribution of multistage purification cell arrangement (comprising above-mentioned concrete structure) continuous arrangement can treat purify air carry out multistage (i.e. many ripples time), continuous, carry out purifying containing multicomponent air scale of construction gas, enrichment and settlement treatment.
6, wherein: the clean unit device being positioned at least significant end is also provided with gas-liquid separation chamber successively; Described gas-liquid separation indoor are provided with gas-liquid separation guide plate and gas-liquid separation membrane; Gas-liquid separation membrane is stainless steel nethike embrane or non-woven membrane or activated charcoal membrane; Described gas-liquid separation membrane is laid along the horizontal plane and surface has multiple plicated layer.
Wherein, described gas-liquid separation membrane is laid and surface has multiple plicated layer (namely its cross section is zigzag, and it is for increasing the time of contact of gas and gas-liquid separation membrane) along the horizontal plane.From the isolated gas of gas-liquid separation chamber (gas-liquid mixture still containing a certain amount of steam), enter gas-liquid separation membrane subsequently, after gas-liquid mixture enters gas-liquid separation membrane, most of moisture can postpone along plicated layer and under, gas can pass through gas-liquid separation membrane, completes gas-liquid separation operation; Moisture after isolation along the surface of plicated layer postpone and under time, complete washing away (namely realizing automatic flushing effect by said structure) gas-liquid separation membrane simultaneously.
In sum, the cleaning system that the embodiment of the present invention provides, overcome conventional purification apparatus can not carry out time deep purifying process of many ripples to same gas and the technological deficiency of separation and concentration can not be carried out (comprising complex chemical composition organic gas) different chemical composition in gas, in the structure of impinging stream gas-liquid reactor, adding photocatalyst structure adopts auto purification type catalytic membrane fundamentally to eliminate the possibility of film body pollution, is a feature of the present invention.
Accompanying drawing explanation
Fig. 1 a is the structural representation of shock flow type gas-liquid reaction room of the prior art;
The structural representation of the percussion flow gas purge system that Fig. 1 provides for the embodiment of the present invention one;
The structural representation of the percussion flow gas purge system that Fig. 1 b provides for the embodiment of the present invention one;
The structural representation of the percussion flow gas purge system of the another kind of version that Fig. 1 c provides for the embodiment of the present invention one;
The array structure schematic diagram of the shock flow type gas-liquid reaction room in the percussion flow gas purge system that Fig. 2 provides for the embodiment of the present invention in Fig. 1 one;
Shock flow type gas-liquid reaction room in the percussion flow gas purge system that Fig. 3 provides for the embodiment of the present invention in Fig. 2 one and the assembly structure schematic diagram of modularization magnetic purifier;
Fig. 4 is the plan structure schematic diagram of Fig. 3;
Fig. 5 is another plan structure schematic diagram of Fig. 3;
The structural representation of the gas-liquid separation chamber in the percussion flow gas purge system that Fig. 6 provides for the embodiment of the present invention one;
The plan structure schematic diagram of the gas-liquid separation chamber in the percussion flow gas purge system that Fig. 7 provides for the embodiment of the present invention one;
The structural representation of the percussion flow gas purge system that Fig. 8 provides for the embodiment of the present invention two;
The structural representation of the percussion flow gas purge system that Fig. 9 provides for the embodiment of the present invention three;
The structural representation of the percussion flow gas purge system that Figure 10 provides for the embodiment of the present invention four;
The structural representation of the percussion flow gas purge system that Figure 11 provides for the embodiment of the present invention five;
The structural representation of the percussion flow gas purge system that Figure 12 provides for the embodiment of the present invention six;
The structural representation of convoluted liquid jet pipe in the percussion flow gas purge system that Figure 13 provides for the embodiment of the present invention seven.
Wherein: percussion flow gas purge system 1; Clean unit device 200; First pipeline 300; Shock flow type gas-liquid reaction room 2; Air inlet 21; Exhaust outlet 22; First deflector 23; Head-on collision chamber 24; Second deflector 25; Positive flow passage 26; Reverse flow passage 27; Modularization magnetic purifier 28; Permanent magnet 29; Second tube connector 3; Liquid supply conduit 40; Liquid backflow pipeline 41; Liquid case 42; The pump housing 43; Convoluted liquid jet pipe 5; Spray hole 51; Auto purification type catalytic membrane 6; Prefilter pipeline 10; Gas-liquid separation chamber 11; 3rd deflector 110; Blower fan 12; System host shell 13; Sewage draining valve 130; Ultraviolet disinfecting lamp tube 131; Ozone outlet 132; Tail gas treatment device 133; Refrigeration plant 14; Master control case 15; Inlet valve 16, level control instrument 17; Electrostatic dust-collecting device 18; Ultraviolet lamp 19; Discharge orifice 20.
Detailed description of the invention
Also by reference to the accompanying drawings the present invention is described in further detail below by specific embodiment.
Embodiment one
See Fig. 1, the embodiment of the present invention one provides a kind of percussion flow gas purge system 1, comprise several clean unit devices 200 of arranging separately of order, between adjacent two described clean unit devices 200, be communicated with (i.e. multiple clean unit device 200 on same level direction, sequentially pass through the first pipeline 300 be connected) by the first pipeline 300; The second tube connector 3 of shock flow type gas-liquid reaction room 2 that each described clean unit device 200 comprises upright shock flow type gas-liquid reaction room 2, the shock flow type gas-liquid reaction room 2 of standing upside down and is communicated with upright shock flow type gas-liquid reaction room 2 and stands upside down; Wherein, above-mentioned second tube connector 3 reality turns through 180 degree a kind of tube connector at angle for having; Upright shock flow type gas-liquid reaction room 2, the symmetrical setting of relative second tube connector about 3 in shock flow type gas-liquid reaction room 2 of standing upside down;
Above-mentioned percussion flow gas purge system 1 also comprises liquid supply conduit 40, liquid backflow pipeline 41 and the liquid case 42 for splendid attire polytype reactant liquor; And be also provided with the pump housing 43 in described liquid case 42;
It should be noted that, the above-mentioned liquid case for splendid attire polytype reactant liquor can be reaction liquid box, filtrate tank and ozonic water tank etc. variety classes; Different types of liquid case in said system can be one group or many groups, arranges according to concrete purification demand, can be separate between the liquid case of many group kinds, and wherein filtrate tank can be communicated with ozonic water tank, and all the other various syndetons repeat no longer one by one; Illustrate (assembly for ozonic water tank composition), liquid backflow pipeline 41 usually arrange corresponding with liquid supply conduit 40 is arranged, and for reclaiming the Ozone Water after being sprayed by jet pipe, and be back to (or in other water tanks) in water tank with strainer; Ozone Water after filtration can be transported in ozonic water tank by the pump housing again, Ozone Water is recycled, significantly saves Ozone Water resource, and be beneficial to environmental protection;
One end of described liquid supply conduit 40 is communicated with the pump housing 43 of described liquid case 42 inside, and the other end is provided with convoluted liquid jet pipe 5 capable of circulation, and the positive flow passage 26 be deep in shock flow type gas-liquid reaction room 2 and reverse flow passage 27; One end of described liquid backflow pipeline 41 is communicated with the bottom of described second tube connector 3, and the other end of described liquid backflow pipeline 41 is communicated with described liquid case 42;
Wherein, above-mentioned shock flow type gas-liquid reaction room 2 also has following structure: air inlet 21; Exhaust outlet 22; First deflector 23; Head-on collision chamber 24; Second deflector 25; Positive flow passage 26; Reverse flow passage 27; Modularization magnetic purifier 28; Permanent magnet 29;
Particularly, modularization magnetic purifier 28 is equipped with in positive flow passage 26 and described reverse flow passage 27 described in each (no matter be upright, or stand upside down) shock flow type gas-liquid reaction room 2; Modularization magnetic purifier 28 comprises the permanent magnet 29 of many group arranged opposite distribution; Above-mentioned convoluted liquid jet pipe 5 partially passes through between many group permanent magnets 29; Convoluted liquid jet pipe 5 is provided with the spray hole 51 in line segment shape that multiple length direction along pipe is offered;
Ultraviolet lamp 19 is also provided with in the first pipeline 300 between adjacent two the described clean unit devices 200 of each connection; The end of the shock flow type gas-liquid reaction room 2 of the handstand in each described clean unit device 200 is also provided with auto purification type catalytic membrane 6; Auto purification type catalytic membrane 6 comprises stainless (steel) wire (not shown) and is plated in the titanium dioxide layer (not shown) on stainless (steel) wire.
See Fig. 2 and Fig. 3 the flow direction of air to be clean (direction of arrow namely illustrate), first deflector 23 with the protruding globoidal structure in middle part that the exhaust outlet 22 that shock flow type gas-liquid reaction room 2 comprises gas inlet 21 that housing (not shown) and case top be provided with, bottom is provided with, housing central section are provided with, the flange in the horizontal direction downwards at the two ends of the first deflector, forms head-on collision chamber 24 (i.e. air impingement district) in the bottom of the first deflector; The below of the first deflector is provided with horizontally disposed second deflector 25; The flange at the two ends of the first deflector 23 forms positive flow passage 26 and reverse flow passage 27 with the second deflector 25 of below respectively; The position in the tube wall knee in the exhaust outlet 22 of shock flow type gas-liquid reaction room and upright U-tube road and handstand U-tube road is corresponding (wherein, arrange setting continuously in multiple shock flow type gas-liquid reaction room 2, the A1 such as, illustrated in figure, A2, A3 ... etc. structure);
Modularization magnetic purifier 28 (see also Fig. 5) is equipped with in positive flow passage 26 and reverse flow passage 27 in shock flow type gas-liquid reaction room 2; Modularization magnetic purifier 28 comprises the permanent magnet 29 of many group arranged opposite distribution; Convoluted liquid jet pipe 5 major part is through many group permanent magnets; Convoluted liquid jet pipe 5 (see also Figure 13) is provided with the spray hole 51 (for spraying Ozone Water or reactant liquor) in line segment shape that multiple length direction along pipe is offered.As in Fig. 4, wherein, non-fill area B is fluid circuit (namely B pipe is liquid jet pipe, and wherein the direction of arrow is liquid flow direction), and C region is liquid knockout district, and a-quadrant is air impingement region.Along bursting at the seams property of the length direction jet orifice of B pipe, linear jet flow hole is coaxially arranged in opposite directions.The shape of B pipe can be determined according to the actual service condition of percussion flow contactor, and can be circular, also can be triangle, trapezoidal or other airtight shape.But the jet pipe coaxially arranged in opposite directions, its length, shape, size must be symmetry equivalent.
Separately see Fig. 1, above-mentioned cleaning system also comprises prefilter pipeline 10, and the front end that prefilter pipeline is positioned at whole cleaning system is communicated with; Prefilter pipeline is also provided with pre-treatment purifier (not shown) and oxygen rich gas air inlet and steam air inlet; Pre-treatment purifier inside is provided with shock flow type gas-liquid reaction room 2.
It should be noted that, thisly utilize the multistage purified treatment repeatedly in the shock flow type gas-liquid reaction room of upright shock flow type gas-liquid reaction room and handstand, and in conjunction with multiple treatment facilities, this system architecture is a kind of unprecedented product inherently; Especially the VOC gas purification process for the air scale of construction is particularly evident.
Below the concrete structure of the percussion flow gas purge system that the embodiment of the present invention provides is described further: wherein, it should be noted that, in percussion flow gas purge system, concrete structure and various malformation are all explained in following detailed description of the invention:
Wherein, described first pipeline 300 is the U-tube road (structure as illustrated in Fig. 1) stood upside down or the rectangle tube connector (structure as illustrated in Fig. 2) of turning through 180 degree angle stood upside down.In addition, the second tube connector 3 also can be chosen as upright U-tube road (structure as illustrated in Fig. 1) or upright rectangle tube connector of turning through 180 degree angle.
As the preferred embodiment of one, described liquid case 42 is for splendid attire Ozone Water and/or filtered water and/or reactant liquor; Also comprise Ozone Water Preparation equipment.
As the preferred embodiment of one, above-mentioned percussion flow gas purge system 1 also comprises prefilter pipeline 10, and described prefilter pipeline 10 is positioned at the front end of the most preposition clean unit device and is communicated with this upright shock flow type gas-liquid reaction room; Described prefilter pipeline is also provided with pre-treatment purifier and oxygen rich gas air inlet; Described pre-treatment purifier inside is also provided with described shock flow type gas-liquid reaction room 2.
The structure analyzing above-mentioned percussion flow gas purge system is known: after the gas containing Various Complex chemical composition (being rich in the compositions such as various particulate matter, VOC or SO2) enters the prefilter pipeline 10 of front end at a high speed under the effect of blower fan, successively enter the clean unit device 200 that several orders are arranged separately, enter upright shock flow type gas-liquid reaction room, the shock flow type gas-liquid reaction room of handstand and internal mode blocking magnetic purifier particularly; The enrichment that pre-treatment purifier can be carried out particulate component material by oxygen rich gas; Wherein, the most key is shock flow type gas-liquid reaction room; After gas to be clean carries out gas inlet, first run into first deflector with the protruding globoidal structure in middle part that housing central section is provided with, then promptly to along the first deflector two ends flowing, enter positive flow passage and reverse flow passage subsequently; Meanwhile, under convoluted liquid jet pipe water spray Ozone Water or reactant liquor (often having charged particle and ion in fluid) are subject to the effect of the Lorentz force of magnet assemblies (i.e. the concrete structure of modularization magnetic purifier) in positive flow passage and reverse flow passage, in positive flow passage and reverse flow passage, form orienting enriching rapidly.
Gas-liquid mixture in head-on collision chamber is movement velocity fast (namely ensureing that in air scale of construction gas, trace constituent carries out high speed enrichment) not only, and can realize high speed purifying and sedimentation for the dusty gas of heterogeneity and particle; In addition, the position in exhaust outlet and first pipeline of shock flow type gas-liquid reaction room or the tube wall knee of the second tube connector is corresponding; The gas-liquid mixture flowed out from the exhaust outlet of shock flow type gas-liquid reaction room like this by directly to upper or flow down to the tube wall knee of the first pipeline or the second tube connector, thus completes attachment sedimentation; And then some pollutant in purifying air very significantly.
Be connected because multiple clean unit device 200 sequentially passes through the first pipeline 300 on same level direction; So band purifies air all successively can enter shock flow type gas-liquid reaction room, modularization magnetic purifier and attached wall construction after entering a joint clean unit device at every turn; Distribute that can treat purifies air and carry out by multistage purification cell arrangement (comprising above-mentioned concrete structure) continuous arrangement multistage (i.e. many ripples time), the purification of continuous, the air scale of construction, enrichment and settlement treatment, it is to the VOC purification treatment technology effect of the air scale of construction clearly.
See Fig. 6, gas-liquid separation chamber 11 comprises the 3rd deflector 110 of housing (not shown) and inside; 3rd deflector 110 top has the protruding globoidal structure (in figure, the direction of arrow illustrates the flow direction of gas-liquid mixture) of two laid out in parallel.Preferably, the lower end of the 3rd deflector of gas-liquid separation chamber, its tangent line and vertical line angle are 20 ° ~ 45 °.
About shock flow type gas-liquid reaction room:
The operation principle of this shock flow type gas-liquid reaction room is head-on collision reaction principle.Open water pump and blower fan, see Fig. 3, Fig. 4 and Fig. 5, the liquid of convoluted liquid jet pipe 5 ejection produces blooming in head-on collision chamber, and from left and right, two outlets produce strong fluid head-on collision in opposite directions along coaxial to the first deflector under certain flow rate respectively.Gas because of quality light, during shock, field energy is little, and positive flow infiltrates reverse flow, and reverse flow also infiltrates positive flow simultaneously, and gas produces oscillating movement, some particle in air to be clean is increased, completes granulation process; Liquid is because of quality weight, and during shock, field energy is large, and partially liq molecule forms polarization phenomena; Part Small molecular in air to be clean and solid particle to the hydrone directed movement polarized, can produce absorption and sorption effect.Pernicious gas wherein, as sulfur dioxide, nitrogen oxide and fluid molecule (containing in reactant liquor) the two-forty ground that polarized chemical absorbing occurs react, is finally enriched in liquid, refluxes and enter ozonic water tank or reaction liquid box; Wherein, Ozone Water or reactant liquor and air strong convection collides, Showed Very Brisk, cause catharsis and corresponding chemical reaction fully and can reach quite high effect purification efficiency.
Last gas to be clean is after multistage purification process, then through gas-liquid separation chamber, produce granulation, gas-liquid is separated further, and finally discharging free of contamination gas can carry out free discharge.
About modularization magnetic purifier:
See Fig. 7, modularization magnetic purifier is beyond example in the application of above-mentioned percussion flow gas purge system, this modularization magnetic purifier forms (i.e. magnet assemblies) primarily of many group magnet, and this magnet assemblies can be selected arrangement according to actual conditions or be scattered in polytype; Convoluted liquid jet pipe capable of circulation be capable of circulation, become convoluted be distributed in around magnet assembly, it is utilize Lorentz force effect to implement stronger atomizing (being similar to centrifugal force separate) by the Ozone Water of convoluted liquid jet pipe inspection capable of circulation or reactant liquor at all, the water smoke ozone water mist and reactant liquor that are atomized by force formation formed reacts in same impingement region gas and particle carries out orienting enriching, convective purification, its treatment effect is clearly; Therefore air to be clean can react and enrichment fully in multiple field regions and multiple head-on collision region, such as, adopts high-intensity magnetic field can implement a large amount of enrichments to the particle of PM2.5.
About gas-liquid separation chamber:
Traditional gas-liquid separation chamber's (primary structure is cyclone separator) often adopts centrifugal action to implement to be separated to water and air, it should be noted that, the 3rd deflector in gas-liquid separation chamber in the cleaning system that the embodiment of the present invention provides has special shape structure, and it does not need, and other any equipment is auxiliary just can carry out good gas-liquid separation; Find after deliberation, known see Fig. 6, gas-liquid mixture enter after entering the 3rd deflector there are two laid out in parallel concave shaped cavity in (semiclosed), flowed rapidly to centre by both sides, after flowing to middle position, tip, hydrone changes from small to big, finally because the position of this point point is extremely conducive to sedimentation, the drippage of water droplet; So just can by the special shape structure of the 3rd deflector, realize being separated of hydrone and air; In embodiments of the present invention, although the structure of the 3rd deflector seems simple, the construction profile obtained really is tested by great many of experiments; But the 3rd deflector often with said structure profile could realize efficiently, perfectly gas-liquid separation operation.Fact proved, although the 3rd deflector isolated air humidity in above-mentioned gas-liquid separation chamber is not little, still clearly, especially structure does not need extra to remove care and maintenance gas-liquid separation chamber's effect.
Preferably, the clean unit device 200 being positioned at least significant end is also provided with gas-liquid separation chamber 11, gas-liquid separation membrane (not shown) successively; Described gas-liquid separation indoor are provided with gas-liquid separation membrane.In addition, the clean unit device being positioned at least significant end is also provided with blower fan 12 outward.
It should be noted that, blower fan 12 Main Function that the clean unit device 200 being positioned at least significant end is arranged completes negative pressure ventilation effect (it provides larger power for treating to purify air, and makes it complete multi-staged air purified treatment at high speed in the system that multiple clean unit device 200 connects to form);
It should be noted that, gas-liquid separation membrane is stainless steel nethike embrane or non-woven membrane or activated charcoal membrane; Described gas-liquid separation membrane is laid along the horizontal plane and surface has multiple plicated layer (namely the gas-liquid separation membrane of said structure also can be used for realizing automatic flushing effect, can obviously help above-mentioned cleaning system significantly to promote detergent power and clean-up effect).
Preferably, above-mentioned percussion flow gas purge system 1 also comprises system host shell 13;
Above-mentioned various hold different liquids component medium liquid case 42 and described Ozone Water Preparation equipment to be all arranged on described system host shell 13 inner; The sewage draining valve 130 that the bottom of described liquid case 42 is equipped with.The top of the internal box wall of described liquid case 42 is also provided with ultraviolet disinfecting lamp tube 131.Top for the described liquid case of splendid attire Ozone Water is provided with ozone outlet 132; Described ozone outlet 132 is communicated with tail gas treatment device 133.
In addition, ozonic water tank (namely for holding the liquid case of Ozone Water), water tank with strainer (namely for holding the liquid case of filtered fluid), reaction liquid box (namely for holding the liquid case of reactant liquor) and Ozone Water Preparation equipment are all arranged on system host enclosure; The sewage draining valve 130 that the bottom of ozonic water tank, water tank with strainer and reaction liquid box is equipped with.Ozonic water tank, water tank with strainer and reaction liquid box inner top are also provided with ultraviolet disinfecting lamp tube 131.
It should be noted that, the body structure of system host shell and whole system; It is dispersed with polytype cisten mechanism; Wherein ozonic water tank is mainly used in providing Ozone Water to main filter pipe, and water tank with strainer can reclaim the Ozone Water of backflow, then through metre filter, finally returns and is transported to ozonic water tank, realize recycling of water resource; In addition, reaction liquid box can hold number of chemical reactant liquor, and such as: ammoniacal liquor, it can generate carbon dioxide and water with formaldehyde generation chemical reaction; Also such as: urea, soybean protein, amino acid can react with formaldehyde isopolarity chemical substance, remove VOC gas in air and there is significant effect.
In addition, the particulate in air to be clean, noxious air, pollutant within the specific limits, can be got rid of by Ozone Water; Because above-mentioned all kinds of water tank must can not have the existence of microorganism, therefore sterilization processing can be implemented to the air in above-mentioned water tank by ultraviolet lamp, avoid not containing bacterium etc. in the air after secondary pollution, guarantee purification, therefore above-mentioned cleaning system can meet purification of air requirement (such as: the places such as medicine manufacture, hospital and school) in the higher place of sanitary condition.
Under above-mentioned comparatively significantly physical absorption and the chemisorbed effect of combining, (namely above-mentioned shock flow type gas-liquid reaction room, modularization magnetic purifier, photocatalyst of titanium dioxide structure and attached wall construction contribute to the effect promoting chemisorbed, chemisorbed is again supplementing said physical purification simultaneously), absorption limit, limit is decomposed, and dispels formaldehyde, benzene, dimethylbenzene, toluene, (indoor total volatile organism (being called for short TVOC) is main from paint, aqueous coating, adhesive, cosmetics, washing agent, wood-based plate, wallpaper, carpet etc. for TVOV.The TVOC found in indoor nearly several thousand kinds, the pernicious gas such as such as: alkanes, aromatic hydrocarbons, alkene class, halogen alkene class, ester class, aldehydes, ketone), generate water and carbon dioxide, secondary pollution is not produced in catalytic reaction process, its the most key ground can fast and effeciently be removed indoor has toxin biology, dust, smoke, stink, virus etc., and produces a large amount of fresh airs (namely having quick and a large amount of distinguishing features).
Ozone outlet 132 is communicated with tail gas treatment device 133.Tail gas treatment device is for removing the ozone gas (avoiding ozone gas discharge to pollute air) in tail gas.
In addition, in embodiments of the present invention, in above-mentioned percussion flow gas purge system, also following structure be may comprise, refrigeration plant 14, master control case 15 and inlet valve 16, level control instrument 17 etc. such as, in system host shell, are also provided with; Wherein, due to needs preparation Ozone Water, prepare Ozone Water simultaneously and need there is certain requirement to its temperature, therefore above-mentioned refrigeration plant may be used for freezing to water; Then implement ozone gas preparation to oxygen rich gas as source of the gas by ozone generator (i.e. the concrete structure of Ozone Water Preparation equipment), said structure is not that modified node method of the present invention repeats no longer one by one to this embodiment of the present invention.
Embodiment two
The concrete structure of the percussion flow gas purge system that the embodiment of the present invention two provides is identical with embodiment one, but its layout type is different, specifically refer to Fig. 8, the percussion flow gas purge system that embodiment two is illustrated, the distribution sequence of its each water tank and distributing position can the composition of gas to be clean and purification demands and determine with reality as the case may be.
Embodiment three
As shown in Figure 9, the structure of this percussion flow gas purge system is also the one in numerous distortion.
Embodiment four
Figure 10 illustrates the percussion flow gas purge system of the embodiment of the present invention four, and its structure is also the one in numerous distortion, and structure something in common repeats no longer one by one.
Embodiment five
Figure 11 illustrates the percussion flow gas purge system of the embodiment of the present invention five, and its structure is also the one in numerous distortion, and structure something in common repeats no longer one by one.
Embodiment six
As shown in figure 12, the percussion flow gas purge system of the embodiment of the present invention six, the blower fan in its structure can the preposition front end at main filter pipe, and its afterbody has also installed electrostatic dust-collecting device 18 additional in addition; Shock flow type cleaning system also can be mated with electrostatic dust-collecting device with physics magnetic field coupling; The operation principle of above-mentioned electrostatic dust-collecting device utilizes high voltage electric field that flue gas is ionized, the dust in air-flow charged under electric field action with flow separation.This system can adopt the combination of different physics and chemistries to complete according to the characteristic of mist to be clean to carry out being separated and enrichment of the high efficiency air scale of construction to the gas of heterogeneity with the particle in gas.In the impact flow reactor structure of standing upside down, the lowest part of the first deflector is also provided with downward discharge orifice 20 (see also Fig. 2) along casing both sides place; Its effect is that the liquid flowed downward by jet pipe is drained in the second tube connector and flows liquid-return box;
Embodiment seven
As shown in figure 13, the convoluted liquid jet pipe 5 of the embodiment of the present invention seven is also be one in numerous distortion, and its pipeline distribution situation is different from the convoluted liquid jet pipe of anticipating shown in Fig. 4, and the distribution of its pipeline can also have various ways in addition.The shape of B pipe can be determined according to the actual service condition of percussion flow contactor, and can be circular, also can be triangle, trapezoidal or other airtight shape, repeats no longer one by one to this embodiment of the present invention.
The concrete effect of the percussion flow gas purge system that the embodiment of the present invention provides illustrates as follows: catharsis expeditiously; Because the head-on collision district of gas and the Hui San district of liquid coincide, gas produces oscillating movement, under the effect of field energy, the solid particle in air, oil droplet and pernicious gas can directly, rapidly with liquid generation chemical reaction, thus reach the object of the efficient harmful substance removed in air.Reaction rate is high; In this equipment reaction set of regions, reaction rate is high.Through test, it has higher mass tranfer coefficient, and lower than power consumption, and your pupil of its reaction speed is to complete air-polluting purification.
The percussion flow gas purge system that the embodiment of the present invention provides for being separated of heterogeneity in air and solid particle, enrichment, especially can arrive high speed, heterogeneity, the air scale of construction, purification of air.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for a person skilled in the art, the present invention can have various modifications and variations.Within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (9)
1. a percussion flow gas purge system, is characterized in that, comprises the clean unit device that several orders are arranged separately, by the first pipeline communication between adjacent two described clean unit devices; Each described clean unit device comprise upright shock flow type gas-liquid reaction room, handstand shock flow type gas-liquid reaction room and be communicated with second tube connector of shock flow type gas-liquid reaction room of upright shock flow type gas-liquid reaction room, handstand; Described second tube connector is turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction room, the shock flow type gas-liquid reaction room of handstand are relative to the second symmetrical setting in tube connector left and right;
Also comprise liquid supply conduit, liquid backflow pipeline and the liquid case for splendid attire polytype reactant liquor; And be also provided with the pump housing in described liquid case;
One end of described liquid supply conduit is communicated with the pump housing of described liquid case inside, and the other end is provided with convoluted liquid jet pipe capable of circulation, and is deep into positive flow passage and the reverse flow passage of shock flow type gas-liquid reaction indoor; One end of described liquid backflow pipeline is communicated with the bottom of described second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
Also ultraviolet lamp is provided with in the first pipeline between adjacent two the described clean unit devices of each connection;
The end of the shock flow type gas-liquid reaction room of the handstand of each described clean unit device is also provided with auto purification type catalytic membrane; Described auto purification type catalytic membrane comprises stainless (steel) wire and is plated in the titanium dioxide layer on described stainless (steel) wire;
The clean unit device being positioned at least significant end is also provided with gas-liquid separation chamber successively; Described gas-liquid separation indoor are provided with gas-liquid separation guide plate and gas-liquid separation membrane.
2. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Modularization magnetic purifier is equipped with in positive flow passage described in described shock flow type gas-liquid reaction room and described reverse flow passage; Described modularization magnetic purifier comprises the permanent magnet of many group arranged opposite distribution; Described convoluted liquid jet tube portion is through many group permanent magnets; Described convoluted liquid jet pipe is provided with the spray hole in line segment shape that multiple length direction along pipe is offered.
3. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Described first pipeline is the rectangle tube connector of turning through 180 degree angle of U-tube road or the handstand of standing upside down;
Described second tube connector is upright U-tube road or upright rectangle tube connector of turning through 180 degree angle.
4. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Described liquid case is used for splendid attire Ozone Water and/or filtered water and/or reactant liquor;
Also comprise Ozone Water Preparation equipment.
5. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Also comprise prefilter pipeline, described prefilter pipeline is positioned at the front end of the most preposition clean unit device and is communicated with this upright shock flow type gas-liquid reaction room; Described prefilter pipeline is also provided with pre-treatment purifier and oxygen rich gas air inlet and steam air inlet;
Described pre-treatment purifier inside is also provided with described shock flow type gas-liquid reaction room.
6. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Described gas-liquid separation membrane is stainless steel nethike embrane or non-woven membrane or activated charcoal membrane; Described gas-liquid separation membrane is laid along the horizontal plane and surface has multiple plicated layer.
7. percussion flow gas purge system as claimed in claim 4, is characterized in that,
The clean unit device being positioned at least significant end is also provided with blower fan outward, and is connected with system.
8. percussion flow gas purge system as claimed in claim 7, is characterized in that,
Also comprise system host shell;
Described liquid case and described Ozone Water Preparation equipment are all arranged on described system host enclosure; The sewage draining valve that the bottom of described liquid case is equipped with;
The top of the internal box wall of described liquid case is also provided with ultraviolet disinfecting lamp tube.
9. percussion flow gas purge system as claimed in claim 4, is characterized in that,
Top for the described liquid case of splendid attire Ozone Water is provided with ozone outlet;
Described ozone outlet is communicated with ozone tail gas treatment facility.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410366353.3A CN104128059B (en) | 2014-07-29 | 2014-07-29 | Percussion flow gas purge system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410366353.3A CN104128059B (en) | 2014-07-29 | 2014-07-29 | Percussion flow gas purge system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104128059A CN104128059A (en) | 2014-11-05 |
| CN104128059B true CN104128059B (en) | 2015-11-25 |
Family
ID=51801070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410366353.3A Expired - Fee Related CN104128059B (en) | 2014-07-29 | 2014-07-29 | Percussion flow gas purge system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104128059B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104923060B (en) * | 2015-04-21 | 2017-05-03 | 江苏大学 | VOCs removing method based on free radical advanced oxidation |
| CN106215484A (en) * | 2016-07-23 | 2016-12-14 | 安徽乙地生态科技有限公司 | A kind of cyanophyceae segregation apparatus for sewage disposal |
| CN106474845A (en) * | 2016-12-05 | 2017-03-08 | 游伟志 | Wet impact stream fume purifier of fume |
| CN106853332A (en) * | 2017-03-03 | 2017-06-16 | 南京嘉源润新环保科技有限公司 | The micro-nano ozone emission-reducing system of waste gas |
| CN108585237A (en) * | 2018-06-25 | 2018-09-28 | 浙江明烁节能科技股份有限公司 | Ecological oxygenation purifies integral type processing system |
| CN110732221B (en) * | 2019-11-19 | 2020-08-07 | 盐城市迎凯涂装设备有限公司 | Coating waste gas treatment system and treatment process |
| CN111790248B (en) * | 2020-07-13 | 2022-07-29 | 上海卓鼎模具有限公司 | Constant-temperature purification air inlet device and system thereof |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2416195A1 (en) * | 1973-04-05 | 1974-10-24 | Universal Oil Prod Co | DUST FILTER |
| CN202315674U (en) * | 2011-09-29 | 2012-07-11 | 赤峰瑞阳化工有限公司 | Waste gas treatment device |
| CN202538591U (en) * | 2012-04-23 | 2012-11-21 | 柯顺雄 | High-efficiency environment-friendly waste gas treatment device |
| CN102824825A (en) * | 2012-09-12 | 2012-12-19 | 无锡光初科技服务有限公司 | Multi-effect U-shaped tube type dedusting and desulfurization integrated device of coal-fired boiler and dedusting and desulfurization method thereof |
| CN202823137U (en) * | 2012-08-02 | 2013-03-27 | 桂林市世环废气处理设备有限公司 | Low-temperature plasma oxygenizer and low-temperature plasma deodorization system |
| CN202983505U (en) * | 2012-12-12 | 2013-06-12 | 国电科学技术研究院 | Two-way smoke demisting device in desulfurizing absorption tower |
| CN203231420U (en) * | 2013-04-10 | 2013-10-09 | 长沙驷马机械制造有限公司 | Pure natural air purifier |
| CN203954985U (en) * | 2014-07-29 | 2014-11-26 | 罗建民 | Percussion flow gas purge system |
-
2014
- 2014-07-29 CN CN201410366353.3A patent/CN104128059B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2416195A1 (en) * | 1973-04-05 | 1974-10-24 | Universal Oil Prod Co | DUST FILTER |
| CN202315674U (en) * | 2011-09-29 | 2012-07-11 | 赤峰瑞阳化工有限公司 | Waste gas treatment device |
| CN202538591U (en) * | 2012-04-23 | 2012-11-21 | 柯顺雄 | High-efficiency environment-friendly waste gas treatment device |
| CN202823137U (en) * | 2012-08-02 | 2013-03-27 | 桂林市世环废气处理设备有限公司 | Low-temperature plasma oxygenizer and low-temperature plasma deodorization system |
| CN102824825A (en) * | 2012-09-12 | 2012-12-19 | 无锡光初科技服务有限公司 | Multi-effect U-shaped tube type dedusting and desulfurization integrated device of coal-fired boiler and dedusting and desulfurization method thereof |
| CN202983505U (en) * | 2012-12-12 | 2013-06-12 | 国电科学技术研究院 | Two-way smoke demisting device in desulfurizing absorption tower |
| CN203231420U (en) * | 2013-04-10 | 2013-10-09 | 长沙驷马机械制造有限公司 | Pure natural air purifier |
| CN203954985U (en) * | 2014-07-29 | 2014-11-26 | 罗建民 | Percussion flow gas purge system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104128059A (en) | 2014-11-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104128059B (en) | Percussion flow gas purge system | |
| CN107789970B (en) | Box air purifier | |
| CN208436600U (en) | A kind of bituminous mixing plant exhaust treatment system | |
| CN103990340A (en) | Wet-type air purifying device and air purifying method | |
| US10722606B2 (en) | Method and device for producing negative oxygen ions, and method and device for purifying air | |
| CN105311931B (en) | Industrial VOCs exhaust gas decomposing, purifying processing method and equipment | |
| CN204799049U (en) | Wet process micron order particulate matter entrapment air purification device | |
| CN204534846U (en) | Air comprehensive purification adjusting device | |
| CN208660820U (en) | A kind of lacquer spraying technique photocatalysis deodorizing device | |
| KR101401992B1 (en) | Scrubber with multi-filtering system | |
| JP2007237101A (en) | Air cleaning apparatus and coating equipment | |
| CN103925651A (en) | Laboratory air purifier and air purifying method based on same | |
| CN106925054A (en) | Gas purge system | |
| CN107497278A (en) | Horizontal exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
| CN205199268U (en) | Industry VOCs waste gas decomposes purifier treatment equipment | |
| CN104998511A (en) | Tail gas purification and environmental protection treatment system of cremator | |
| CN203954985U (en) | Percussion flow gas purge system | |
| CN202803044U (en) | Air purifier | |
| KR102116381B1 (en) | Wet air purification system for Public use facilities | |
| CN205965456U (en) | Organic waste gas integrated treating equipment | |
| CN102836611A (en) | Air purification device | |
| CN107511051A (en) | Vertical exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
| CN205127715U (en) | Novel pressure -fired air purification device | |
| CN206604323U (en) | A kind of gas purge system | |
| CN207413050U (en) | A kind of paint exhaust treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151125 Termination date: 20170729 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |