CN104128059A - Impinging stream gas purification system - Google Patents
Impinging stream gas purification system Download PDFInfo
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- CN104128059A CN104128059A CN201410366353.3A CN201410366353A CN104128059A CN 104128059 A CN104128059 A CN 104128059A CN 201410366353 A CN201410366353 A CN 201410366353A CN 104128059 A CN104128059 A CN 104128059A
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Abstract
The invention discloses an impinging stream gas purification system, including a plurality of purification unit devices at intervals in order. Two adjacent purification unit devices are communicated through a first pipeline; each purification unit device comprises an upright impinging flow type gas-liquid reaction chamber, an inverted impinging flow type gas-liquid reaction chamber and a second pipeline for communication; a convolute liquid jet pipe inserts into a forward flow channel and a reverse flow channel in the impinging stream type gas-liquid reaction chamber; the first pipeline between the two adjacent purification unit devices is provided with an ultraviolet lamp; the end of the inverted impinging flow type gas-liquid reaction chamber in each purification unit device is also provided with a self-cleaning catalytic membrane; the self-cleaning catalytic membrane includes a stainless steel mesh and a titanium dioxide layer plated on the stainless steel mesh; the purification unit device at the extreme end is orderly provided with a gas-liquid separation chamber; and the gas-liquid separation chamber is provided with a gas-liquid separation guide plate and a gas-liquid separation membrane. The system can carry out high efficiency purification treatment on gas in a large amount of and containing various ingredients.
Description
Technical field
The present invention relates to air cleaning facility field, relate in particular to a kind of percussion flow gas purge system.
Background technology
Urban air-quality worse and worse now, people are also more and more stronger to improving the demand of air quality, people are for pm2.5 (particulate matter, particle), be the particle that in surrounding air, aerodynamics equivalent diameter is less than or equal to 2.5 μ m (micron), also claim fine particle.This numerical value of pm2.5 is higher just represents that air pollution is more serious.Yet in daily industrial production, the gas that usually can discharge a large amount of heterogeneities causes (comprising solid particle, dust, organic pollutant of polluting class etc.) pollution of air;
Air purifier is classified and is had three kinds by cleaning principle:
1, filter absorbent-type: utilize porous filtering material, as nonwoven, filter paper, fiber, foam cotton etc. (HEPA high-density air filter material is counted in working as that adsorption capacity is the strongest at present), the suspended particulate in absorbed air, pernicious gas, thus purify air.2, electrostatic precipitation type: make pollutants in air charged by static, then adsorbed the dirt in air of charged particle with dust collect plant trapping, reach the object that purifies air.3, compound: to utilize filtration and electrostatic precipitation mode to purify air simultaneously.
Wherein: filter absorbent-type, for example: (1) adopts and considers material, consider plate, filter cylinders etc. have (it are comparatively obvious for particle enrichment) such as type gas film or active carbons, but of long duration, the film body of gas film is bound to by the Particulate Pollution after enrichment, thereby the air after its processing causes secondary pollution, and the film body of this gas film non-renewable (because of its particle adhering to often very little, composition is very complicated, but the gas film after cleaning equally also adheres to such particle, cannot continue to use), it is more aobvious helpless to the atmosphere scale of construction and multicomponent gas cleaning for what is more important.
Wherein, its processing gaseous substance of electrostatic gas purifying equipment is very single, to VOC, can not effectively be removed.
Wherein, in compound gas purifying equipment, mainly adopt filtrate prepare filter screen or filter cylinder and in conjunction with electrostatic apparatus, airborne particle carried out to enrichment; Or (VOC material refers to the general name of holding at normal temperatures volatile organic substance, common are formaldehyde, toluene and dimethylbenzene etc. to the VOC gas that contains of seldom a part of little gas flow to adopt some polar substances (for example: sulphur fiber soaks profound some chemical substance).) degrade and remove; But still there is the technological deficiency of following several aspects in it: when gas film and the use of electrostatic depuration structure composite, windage is larger, it can not carry out high efficiency purification to the gas of the atmosphere scale of construction, treating capacity is very little, in air, still existing a large amount of polluters can not be purified, and its purified treatment efficiency is very low.It processes gas componant few; For example the middle sulfur dioxide of 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 (being that number of patent application is 03102035.6), its primary structure comprises anterior shock flow type gas-liquid reaction chamber 2 and the gas-liquid separation chamber at rear portion, wherein; The shock flow type gas-liquid reaction chamber 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 clashing), and its bottom is impingement region outlet (being exhaust outlet 22); In the space in Gai air impingement district, at least one pair of jet pipe is set; This arranges 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 of deflector III, form both sides gas discharge outlet, and in formation gas collection district, top, the middle part in this gas collection district is provided with outlet, this technical scheme has following characteristics, and this scheme provides a kind of high speed, initiatively, gas-liquid reactor, can within a short period of time to carrying out reaction that efficiency is higher compared with the atmosphere scale of construction and different trace constituents in gas being carried out to separated and enrichment.This scheme has following deficiency: 1. pair pending gas has only carried out gas-liquid contact one time, can not carry out the gas-liquid contact of the degree of depth and Duo Bo time.2. can only adopt a kind of liquid as gas-liquid contact media, can not carry out reaction and separation processes enrichment processing to the gas containing multiple heterogeneity.3. this technical scheme can not form efficiency light catalyst structure, thereby the efficiency when carrying out chemical reaction containing the gas of different chemical composition is very low.
Summary of the invention
The object of the present invention is to provide a kind of percussion flow gas purge system, to address the above 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 arrange separately, between adjacent two described clean unit devices, pass through the first pipeline communication; Described in each, clean unit device comprises the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand and the second tube connector that is communicated with the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand; Described the second tube connector is to turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction chamber, relative the second symmetrical setting in tube connector left and right in the shock flow type gas-liquid reaction chamber of handstand;
Also comprise liquid supply conduit, liquid backflow pipeline and for the liquid case of 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 convolution shape liquid jet pipe capable of circulation, and is deep into the indoor positive flow passage of shock flow type gas-liquid reaction and reverse flow passage; One end of described liquid backflow pipeline is communicated with the bottom of described the second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
Each is communicated with in the first pipeline between adjacent two described clean unit devices and is also provided with ultraviolet lamp;
The end of the shock flow type gas-liquid reaction chamber of the handstand of clean unit device described in each 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 that is positioned at least significant end is also provided with gas-liquid separation chamber successively; Indoor gas-liquid separation guide plate and the gas-liquid separation membrane of being provided with of described gas-liquid separation.
Preferably, in positive flow passage described in described shock flow type gas-liquid reaction chamber and described reverse flow passage, be equipped with modularization magnetic purifier; Described modularization magnetic purifier comprises the permanent magnet of the relative arranged distribution of many groups; Described convolution shape liquid jet tube portion is through between many group permanent magnets; Described convolution shape liquid jet pipe is provided with a plurality of spray holes that are line segment shape of offering along the length direction of pipe.
Compared with prior art, the advantage of the embodiment of the present invention is:
Analyze above-mentioned air purification structure known: the main improvement structure of above-mentioned percussion flow gas purge system is:
1, the clean unit device that several orders arrange separately, the first pipeline communication is passed through at the top (or top) between adjacent two described clean unit devices, thereby forms continuous multistage purification equipment;
2, described in each, clean unit device comprises the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand and the second tube connector that is communicated with the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand; Described the second tube connector is to turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction chamber, relative the second symmetrical setting in tube connector left and right in the shock flow type gas-liquid reaction chamber of handstand;
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 by turning through 180 degree second tube connector at angle, connect and compose the symmetrical setting in left and right, shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand.
3, each is communicated with in the first pipeline between adjacent two described clean unit devices and is also provided with ultraviolet lamp; The end of the shock flow type gas-liquid reaction chamber of the handstand of clean unit device described in each 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 has stronger oxidation and reducing power can be oxidized by force and reduction reaction VOC (being mainly organic matter volatile matter), the large molecule of VOC is converted into small-molecule substance (for example carbon dioxide and water) after above-mentioned reaction; And produce a large amount of negative oxygen ions.It should be noted that, set ultraviolet lamp and the set catalytic membrane of last reactor end in the first pipeline, is a kind of photocatalyst structure necessary condition each other.This structure toxic and harmful in air of effectively degrading; Can effectively 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 be optimized air quality, and the air ambient of a high-quality is provided.
4, also comprise liquid supply conduit, liquid backflow pipeline and for the liquid case of 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 convolution shape liquid jet pipe capable of circulation, and is deep into the indoor positive flow passage of shock flow type gas-liquid reaction and reverse flow passage; One end of described liquid backflow pipeline is communicated with the bottom of described the second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
In positive flow passage described in described shock flow type gas-liquid reaction chamber and described reverse flow passage, be equipped with modularization magnetic purifier; Described modularization magnetic purifier comprises the permanent magnet of the relative arranged distribution of many groups; Described convolution shape liquid jet tube portion is through between many group permanent magnets; Described convolution shape liquid jet pipe is provided with a plurality of spray holes that are line segment shape of offering along the length direction of pipe.
In said process, when gas enters shock flow type gas-liquid reaction chamber, (it has comprised polytype solution for one end of liquid supply conduit and liquid case, such as Ozone Water, filtered water, reactant liquor etc.) the inner pump housing is communicated with, the other end is provided with convolution shape liquid jet pipe capable of circulation, and is deep into the indoor positive flow passage of shock flow type gas-liquid reaction and reverse flow passage; Above-mentioned gas can be implemented fluid purification operation in the indoor positive flow passage of shock flow type gas-liquid reaction and reverse flow passage;
The gas of discharging from the impingement region outlet of upright shock flow type gas-liquid reaction chamber first declines through the bottom of the second tube connector, then the gas that (this process passed through turn through 180 degree place, angle) enter rapidly the shock flow type gas-liquid reaction chamber 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, in positive flow passage described in shock flow type gas-liquid reaction chamber and reverse flow passage, be equipped with modularization magnetic purifier.
The operation principle of analyzing above-mentioned percussion flow gas purge system is known: the gas that contains Various Complex chemical composition (being rich in the compositions such as various particulate matters, VOC or SO2) first at a high speed enters pre-treatment purifier under the effect of blower fan, and pre-treatment purifier carries out enrichment, sedimentation to particulate matter percussion flow gas liquid reaction is indoor by oxygen rich gas and high-temperature steam; Then pending gas enters immediately and in several continuous clean unit devices, carries out gas purification many ripples time, high-speed and continuous; When entering each clean unit device, all successively enter upright shock flow type gas-liquid reaction chamber and the modularization magnetic purifier of inside and the shock flow type gas-liquid reaction chamber of the second tube connector and handstand; And on catalytic membrane surface, be oxidized and reduction reaction under the irradiation of ultraviolet lamp by catalytic membrane.Concrete condition: the gas that gas to be clean enters upright shock flow type gas-liquid reaction chamber enters after mouth, first run into first deflector with the protruding globoidal structure in middle part that housing middle part is provided with, then promptly to flowing along the first deflector two ends, enter subsequently positive flow passage and reverse flow passage; In positive flow passage and reverse flow passage after magnetic purifying is processed, enter air impingement district; Gas-liquid mixture in air impingement district is movement velocity fast (guaranteeing that in atmosphere scale of construction gas, trace constituent carries out high speed enrichment) not only, and can realize high speed purifying and sedimentation for dusty gas and the particle of heterogeneity; In addition, the impingement region outlet of upright shock flow type gas-liquid reaction chamber arranges 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 turning fast rise enters the shock flow type gas-liquid reaction chamber (simultaneously completing knock-on reaction) of handstand subsequently;
Wherein: modularization magnetic purifier is when magnetic purifying is processed, in positive flow passage and reverse flow passage, circle round shape liquid jet pipe jetting liquid (for example: Ozone Water or reactant liquor, the liquid of these injections will carry out purified treatment to air), and in liquid, often there is charged particle and ion) be subject under the effect of Lorentz force of magnet assemblies (being the concrete structure of modularization magnetic purifier), at positive flow passage and the motion of reverse flow passage interior orientation, form particle enrichment region rapidly, this enrichment region and impingement region are overlapping, have strengthened 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 has strengthened enrichment and the infall process of chemical reaction process and particle.
Due in same level direction, by a plurality of clean unit installation compositions separately multistage purification equipment; So air to be clean all can successively enter upright shock flow type gas-liquid reaction chamber, 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 chamber of handstand, modularization magnetic purifier; With the photocatalyst structure being formed by catalytic membrane and ultraviolet lamp.Due to multistage purification cell arrangement (comprising above-mentioned concrete structure) continuous arrangement distribute that can treat purifies air and carry out multistage (being many ripples), continuously, contain that multicomponent atmosphere scale of construction gas purifies, enrichment and sedimentation process.
6, wherein: the clean unit device that is positioned at least significant end is also provided with gas-liquid separation chamber successively; Indoor gas-liquid separation guide plate and the gas-liquid separation membrane of being provided with of described gas-liquid separation; Gas-liquid separation membrane is stainless steel nethike embrane or non-woven membrane or activated charcoal membrane; Described gas-liquid separation membrane has a plurality of plicated layers along horizontal plane laying and surface.
Wherein, described gas-liquid separation membrane has a plurality of plicated layers (be that its cross section is zigzag, it is for increasing the time of contact of gas and gas-liquid separation membrane) along horizontal plane laying and surface.From the isolated gas of gas-liquid separation chamber (gas-liquid mixture that still contains a certain amount of steam), enter subsequently gas-liquid separation membrane, gas-liquid mixture enters after gas-liquid separation membrane, most of moisture can along plicated layer postpone and under, gas can pass through gas-liquid separation membrane, completes gas-liquid separation operation; Moisture after separation is postponed and lower time along the surface of plicated layer, has completed wash away (the realizing automatic flushing effect by said structure) to gas-liquid separation membrane simultaneously.
In sum, the cleaning system that the embodiment of the present invention provides, having overcome conventional purification apparatus can not carry out time deep purifying processing of many ripples and can not to different chemical composition in gas, carry out (comprising complex chemical composition organic gas) technological deficiency of separation and concentration same gas, in the structure of impinging stream gas-liquid reactor, adding photocatalyst structure to adopt auto purification type catalytic membrane fundamentally to eliminate the possibility that film body pollutes, is a feature of the present invention.
Accompanying drawing explanation
Fig. 1 a is the structural representation of shock flow type gas-liquid reaction of the prior art chamber;
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 chamber 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 chamber 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 shape liquid jet pipe circles round 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; The first pipeline 300; Shock flow type gas-liquid reaction chamber 2; Air inlet 21; Exhaust outlet 22; The first deflector 23; Head-on collision chamber 24; The second deflector 25; Positive flow passage 26; Reverse flow passage 27; Modularization magnetic purifier 28; Permanent magnet 29; The second tube connector 3; Liquid supply conduit 40; Liquid backflow pipeline 41; Liquid case 42; The pump housing 43; Convolution shape liquid jet pipe 5; Spray hole 51; Auto purification type catalytic membrane 6; Preposition filter pipe 10; Gas-liquid separation chamber 11; The 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.
The specific embodiment
Below by specific embodiment, also by reference to the accompanying drawings the present invention is described in further detail.
Embodiment mono-
Referring to Fig. 1, the embodiment of the present invention one provides a kind of percussion flow gas purge system 1, comprise the clean unit device 200 that several orders arrange separately, between adjacent two described clean unit devices 200, by the first pipeline 300, be communicated with (being that a plurality of clean unit devices 200 are connected by the first pipeline 300 at same level side's upstream sequence); Described in each, clean unit device 200 comprises upright shock flow type gas-liquid reaction chamber 2, the shock flow type gas-liquid reaction chamber 2 of standing upside down and is communicated with upright shock flow type gas-liquid reaction chamber 2 and the second tube connector 3 of the shock flow type gas-liquid reaction chamber 2 of handstand; Wherein, above-mentioned the second tube connector 3 is actual turns through 180 degree a kind of tube connector at angle for having; Upright shock flow type gas-liquid reaction chamber 2, the relative second tube connector 3 symmetrical settings in left and right in shock flow type gas-liquid reaction chamber 2 of standing upside down;
Above-mentioned percussion flow gas purge system 1 also comprises liquid supply conduit 40, liquid backflow pipeline 41 and for the liquid case 42 of 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, filtered fluid case and ozonic water tank etc. variety classes; Different types of liquid case in said system can be one group or many groups, according to concrete purification demand, arranges, and organize can be separate between the liquid case of kind more, and wherein filtered fluid case can be communicated with ozonic water tank, and all the other various syndetons repeat no longer one by one; Illustrate (assembly that the ozonic water tank of take forms is example), common the arrange setting corresponding with liquid supply conduit 40 of liquid backflow pipeline 41, and for reclaiming the Ozone Water after being sprayed by jet pipe, and be back to water tank with strainer interior (or in other water tanks); The pump housing can be transported to the Ozone Water after filtering in ozonic water tank again, and Ozone Water is recycled, and has significantly saved Ozone Water resource, and has been 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 convolution shape liquid jet pipe 5 capable of circulation, and is deep into positive flow passage 26 and the reverse flow passage 27 in shock flow type gas-liquid reaction chamber 2; One end of described liquid backflow pipeline 41 is communicated with the bottom of described the 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 chamber 2 also has following structure: air inlet 21; Exhaust outlet 22; The first deflector 23; Head-on collision chamber 24; The second deflector 25; Positive flow passage 26; Reverse flow passage 27; Modularization magnetic purifier 28; Permanent magnet 29;
Particularly, described in each (no matter be upright, still stand upside down) shock flow type gas-liquid reaction chamber 2, in positive flow passage 26 and described reverse flow passage 27, be equipped with modularization magnetic purifier 28; Modularization magnetic purifier 28 comprises the permanent magnet 29 of the relative arranged distribution of many groups; Above-mentioned convolution shape liquid jet pipe 5 parts are through between many group permanent magnets 29; Convolution shape liquid jet pipe 5 is provided with a plurality of spray holes that are line segment shape 51 of offering along the length direction of pipe;
Each is communicated with in the first pipeline 300 between adjacent two described clean unit devices 200 and is also provided with ultraviolet lamp 19; The end of the shock flow type gas-liquid reaction chamber 2 of the handstand described in each in 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.
Referring to Fig. 2 and Fig. 3 the flow direction of air to be clean (direction of arrow illustrate), shock flow type gas-liquid reaction chamber 2 comprises the gas inlet 21 that housing (not shown) and case top be provided with, the exhaust outlet 22 that bottom is provided with, first deflector 23 with the protruding globoidal structure in middle part that housing middle part is provided with, the flange of along continuous straight runs downwards at the two ends of the first deflector, forms head-on collision chamber 24 (being air impingement district) in the bottom of the first deflector; The below of the first deflector is provided with horizontally disposed the 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 exhaust outlet 22 of shock flow type gas-liquid reaction chamber is corresponding (wherein with the position in the tube wall knee of upright U-shaped pipeline and the U-shaped pipeline that stands upside down, a plurality of shock flow type gas-liquid reactions chamber 2 setting of arranging continuously, the A1 for example illustrating in figure, A2, A3 ... etc. structure);
In shock flow type gas-liquid reaction chamber 2, in positive flow passage 26 and reverse flow passage 27, be equipped with modularization magnetic purifier 28 (separately referring to Fig. 5); Modularization magnetic purifier 28 comprises the permanent magnet 29 of the relative arranged distribution of many groups; Convolution shape liquid jet pipe 5 is most of through between many group permanent magnets; Convolution shape liquid jet pipe 5 (separately referring to Figure 13) are provided with a plurality of spray holes that are line segment shape 51 of offering along the length direction of pipe (for spraying Ozone Water or reactant liquor).In Fig. 4, wherein, fill area B is not fluid circuit (be that B pipe is liquid jet pipe, 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 orifice coaxially arranges in opposite directions.The shape of B pipe can be determined according to the actual service condition of percussion flow contactor, can be circular, can be also triangle, trapezoidal or other airtight shape.But the coaxial jet pipe arranging in opposite directions, its length, shape, big or small necessary symmetry equivalent.
Separately see Fig. 1, above-mentioned cleaning system also comprises preposition filter pipe 10, and the front end that preposition filter pipe is positioned at whole cleaning system is communicated with; On preposition filter pipe, be 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 chamber 2.
It should be noted that, this multistage purified treatment repeatedly in shock flow type gas-liquid reaction chamber of utilizing upright shock flow type gas-liquid reaction chamber and handstand, and in conjunction with multiple treatment facilities, this system architecture itself is exactly a kind of unprecedented product; Especially for the VOC gas purification of the atmosphere scale of construction, process particularly evident.
The concrete structure of the percussion flow the gas purge system below embodiment of the present invention being provided is described further: wherein, it should be noted that, in percussion flow gas purge system, concrete structure and various malformation are all explained in the following specific embodiment:
Wherein, described the first pipeline 300 is the U-shaped pipeline (as the structure of illustrating in Fig. 1) that stands upside down or the rectangle tube connector (as the structure of illustrating in Fig. 2) of turning through 180 degree angle that stands upside down.In addition, the second tube connector 3 also can be chosen as upright U-shaped pipeline (as the structure of illustrating in Fig. 1) or upright rectangle tube connector of turning through 180 degree angle.
As a kind of preferred embodiment, 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 a kind of preferred embodiment, above-mentioned percussion flow gas purge system 1 also comprises preposition filter pipe 10, and described preposition filter pipe 10 is positioned at the front end of the most preposition clean unit device and the shock flow type gas-liquid reaction chamber upright with this is communicated with; On described preposition filter pipe, be 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 chamber 2.
The structure of analyzing above-mentioned percussion flow gas purge system is known: the gas that contains Various Complex chemical composition (being rich in the compositions such as various particulate matters, VOC or SO2) enters after the preposition filter pipe 10 of front end at a high speed under the effect of blower fan, successively enter the clean unit device 200 that several orders arrange separately, enter particularly shock flow type gas-liquid reaction chamber and the internal mode blocking magnetic purifier of upright shock flow type gas-liquid reaction chamber, handstand; The enrichment that pre-treatment purifier can carry out particulate component material by oxygen rich gas; Wherein, the most key is shock flow type gas-liquid reaction chamber; Gas to be clean carries out after gas inlet, first runs into first deflector with the protruding globoidal structure in middle part that housing middle part is provided with, and then, promptly to flowing along the first deflector two ends, enters subsequently positive flow passage and reverse flow passage; Meanwhile, the shape liquid jet pipe that circles round in positive flow passage and reverse flow passage water spray Ozone Water or reactant liquor (often having charged particle and ion in fluid) are subject to, under the effect of Lorentz force of magnet assemblies (being the concrete structure of modularization magnetic purifier), forming orienting enriching rapidly in positive flow passage and reverse flow passage.
Gas-liquid mixture in head-on collision chamber is movement velocity fast (in guaranteeing atmosphere scale of construction gas, trace constituent carries out high speed enrichment) not only, and can realize high speed purifying and sedimentation for dusty gas and the particle of heterogeneity; In addition, the exhaust outlet of shock flow type gas-liquid reaction chamber is corresponding with the position in the tube wall knee of the first pipeline or the second tube connector; The gas-liquid mixture flowing out from the exhaust outlet of shock flow type gas-liquid reaction chamber like this, by directly flowing to up or down the tube wall knee of the first pipeline or the second tube connector, adheres to sedimentation thereby complete; And then some pollutant in purifying air very significantly.
Because a plurality of clean unit devices 200 are connected by the first pipeline 300 at same level side's upstream sequence; So band purifies air and all can successively enter shock flow type gas-liquid reaction chamber, modularization magnetic purifier and attached wall construction after entering a joint clean unit device at every turn; By multistage purification cell arrangement (comprising above-mentioned concrete structure) continuous arrangement distribute that can treat purifies air and carry out multistage (being many ripples), continuously, purification, enrichment and the sedimentation of the atmosphere scale of construction process, its VOC purification treatment technology effect to the atmosphere scale of construction is very obvious.
Referring to Fig. 6, gas-liquid separation chamber 11 comprises housing (not shown) and the 3rd inner deflector 110; The 3rd deflector 110 tops have two protruding globoidal structures of arranging side by side (in figure the direction of arrow illustrated the flow direction of gas-liquid mixture).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 chamber:
The operation principle of this shock flow type gas-liquid reaction chamber is head-on collision reaction principle.Open water pump and blower fan, referring to Fig. 3, Fig. 4 and Fig. 5, the liquid of convolution shape liquid jet pipe 5 ejections produces blooming in head-on collision chamber, and from left and right, two outlet edges under certain flow rate coaxially produce strong fluid head-on collision to the first deflector in opposite directions respectively.Gas because of quality light, during shock, field energy is little, positive flow is infiltrated reverse flow, reverse flow is also infiltrated positive flow simultaneously, γ-ray emission oscillating movement increases airborne some particle to be clean, completes granulation process; Liquid is because of quality weight, and during shock, field energy is large, and partially liq molecule forms polarization phenomena; The little molecule of airborne part to be clean and solid particle can, to the hydrone directed movement having polarized, produce absorption and sorption effect.Pernicious gas wherein, react as chemical absorbing occurs for sulfur dioxide, nitrogen oxide and fluid molecule (containing in reactant liquor) the two-forty ground that polarized, is finally enriched in liquid, and backflow enters ozonic water tank or reaction liquid box; Wherein, Ozone Water or reactant liquor and the collision of air strong convection, 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 is processed, and Zai Jing gas-liquid separation chamber, produces granulation, and gas-liquid is further separated, finally discharges free of contamination gas and can carry out free discharge.
About modularization magnetic purifier:
Referring to Fig. 7, modularization magnetic purifier is beyond example in the application of above-mentioned percussion flow gas purge system, this modularization magnetic purifier mainly forms (being magnet assemblies) by organizing magnet more, and this magnet assemblies can select to arrange or be scattered in polytype according to actual conditions; Convolution shape liquid jet pipe capable of circulation be capable of circulation, become convolution shape and be distributed in magnet assembly around, it is to utilize Lorentz force effect that the Ozone Water of the convolution shape liquid jet pipe inspection to capable of circulation or reactant liquor are implemented to stronger atomizing (being similar to centrifugal force separate) at all, gas is reacted the water smoke that the ozone water mist that strong atomization is formed and reactant liquor form in same impingement region and particle carries out orienting enriching, convection current purifies, and its treatment effect clearly; Therefore air to be clean can react and enrichment fully in a plurality of field regions and a plurality of head-on collisions region, for example, adopts high-intensity magnetic field to implement a large amount of enrichments to the particle of PM2.5.
About gas-liquid separation chamber:
It is separated that traditional gas-liquid separation chamber (primary structure is cyclone separator) often adopts centrifugal action to implement 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 are auxiliary just can carry out good gas-liquid separation; Find after deliberation, known referring to Fig. 6, gas-liquid mixture enters after entering the 3rd deflector to be had in two concave shaped cavities of arranging side by side (semiclosed), by both sides, to centre, flowed rapidly, behind position, tip in the middle of flowing to, hydrone changes from small to big, and finally due to the position of this point point, is extremely conducive to sedimentation, the drippage of water droplet; So just can pass through the special shape structure of the 3rd deflector, realize the separated of hydrone and air; In embodiments of the present invention, although the structure of the 3rd deflector seems simply, really by great many of experiments, test the construction profile obtaining; Yet the 3rd deflector often with said structure profile could be realized efficiently, perfectly gas-liquid separation operation.Fact proved, although the isolated air humidity of the 3rd deflector in above-mentioned gas-liquid separation chamber is not little, still clearly, especially structure does not need the extra care and maintenance that goes to gas-liquid separation chamber's effect.
Preferably, the clean unit device 200 that is positioned at least significant end is also provided with gas-liquid separation chamber 11, gas-liquid separation membrane (not shown) successively; The indoor gas-liquid separation membrane that is provided with of described gas-liquid separation.In addition, the clean unit device that is positioned at least significant end is also provided with blower fan 12 outward.
It should be noted that, blower fan 12 Main Functions that are positioned at clean unit device 200 settings of least significant end complete negative pressure ventilation effect (it provides larger power for treating to purify air, and makes to complete multi-staged air purified treatment in its system connecting to form at a plurality of clean unit devices 200 at high speed);
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 has a plurality of plicated layers (gas-liquid separation membrane that is 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) along horizontal plane laying and surface.
Preferably, above-mentioned percussion flow gas purge system 1 also comprises system host shell 13;
Above-mentioned various liquid case 42 and the described Ozone Water Preparation equipment that holds different liquids composition medium is all arranged on described system host shell 13 inside; 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.The top that is used 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 (for holding the liquid case of Ozone Water), water tank with strainer (for holding the liquid case of filtered fluid), reaction liquid box (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, system host shell is the body structure of whole system; Its polytype cisten mechanism that distributing; 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 filter, filters, and finally returns and is transported to ozonic water tank, realizes recycling of water resource; In addition, reaction liquid box can hold number of chemical reactant liquor, for example: ammoniacal liquor, it can generate carbon dioxide and water with formaldehyde generation chemical reaction; Also for example: urea, soybean protein, amino acid can react with formaldehyde isopolarity chemical substance, remove VOC gas in air and there is significant effect.
In addition, Ozone Water within the specific limits, can be got rid of airborne particulate to be clean, noxious air, pollutant; Because above-mentioned all kinds of water tanks must be able to not have the existence of microorganism, therefore by ultraviolet lamp, can implement sterilization processing to the air in above-mentioned water tank, avoid secondary pollution, do not contain bacterium etc. in the air after ensure purifying, the air cleaning that therefore above-mentioned cleaning system can meet the place that sanitary condition is higher require (such as: the places such as medicine manufacture, hospital and school).
Under above-mentioned comparatively significantly physical absorption and the chemisorbed effect of combining, (be the effect that above-mentioned shock flow type gas-liquid reaction chamber, modularization magnetic purifier, photocatalyst of titanium dioxide structure and attached wall construction contribute to promote chemisorbed, chemisorbed is again supplementing aforementioned physical cleaning simultaneously), decompose on absorption limit, limit, dispels formaldehyde, benzene, dimethylbenzene, toluene, (indoor total volatile organism (being called for short TVOC) is mainly from paint, aqueous coating, adhesive, cosmetics, washing agent, wood-based plate, wallpaper, carpet etc. for TVOV.At the indoor TVOC having found, reach several thousand kinds, such as alkanes, aromatic hydrocarbons, alkene class, halogen alkene class, ester class, aldehydes, ketone) etc. pernicious gas, generate water and carbon dioxide, in catalytic reaction process, do not produce secondary pollution, indoor have toxin biology, dust, smoke, stink, virus etc. can fast and effeciently be removed in its most key ground, and produce a large amount of fresh air (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 (having avoided ozone gas to discharge pollutes atmosphere) of tail gas.
In addition, in embodiments of the present invention, in above-mentioned percussion flow gas purge system, also may comprise following structure, such as being also provided with refrigeration plant 14, master control case 15 and inlet valve 16, level control instrument 17 etc. in system host shell; Wherein, because needs are prepared Ozone Water, preparing Ozone Water need to have certain requirement to its temperature simultaneously, and therefore above-mentioned refrigeration plant can be for freezing to water; Then by ozone generator (being the concrete structure of Ozone Water Preparation equipment), oxygen rich gas is implemented to ozone gas preparation as source of the gas, said structure is not that improvement structure of the present invention repeats no longer one by one to this embodiment of the present invention.
Embodiment bis-
The concrete structure of the percussion flow gas purge system that the embodiment of the present invention two provides is identical with embodiment mono-, but its layout type is different, specifically refer to Fig. 8, the percussion flow gas purge system of embodiment bis-signal, the distribution sequence of its each water tank and distributing position can be as the case may be determined with the composition of reality gas to be clean and purification demand.
Embodiment tri-
As shown in Figure 9, the structure of this percussion flow gas purge system is also a kind of in numerous distortion.
Embodiment tetra-
Figure 10 illustrates the percussion flow gas purge system of the embodiment of the present invention four, and its structure is also a kind of 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 a kind of 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 can also can be mated with electrostatic dust-collecting device with physics magnetic field coupling; The operation principle of above-mentioned electrostatic dust-collecting device is to utilize high voltage electric field that flue gas is ionized, 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 the gas of heterogeneity is carried out to the separated and enrichment of the high efficiency atmosphere scale of construction 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 (separately referring to Fig. 2) along place, casing both sides; Its effect is that liquid that jet pipe is flowed downward is drained in the second tube connector and flows liquid-return box;
Embodiment seven
As shown in figure 13, the convolution shape liquid jet pipe of the embodiment of the present invention 75 is for being also a kind of in numerous distortion, and its pipeline distribution situation is different from the convolution shape liquid jet pipe of anticipating shown in Fig. 4, and its pipeline distributes in addition can also various ways.The shape of B pipe can be determined according to the actual service condition of percussion flow contactor, can be circular, can be also triangle, and 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 head-on collision district and the liquid Hui San district of gas coincides, γ-ray emission oscillating movement, under the effect of field energy, airborne solid particle, oil droplet and pernicious gas can be directly, rapidly with liquid generation chemical reaction, thereby reach the object of the airborne harmful substance of efficient removal.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 is for separated, the enrichment of heterogeneity in air and solid particle, especially can arrive high speed, heterogeneity, the atmosphere scale of construction, air cleaning.
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 modification of doing, be equal to replacement, improvement etc., within all should being included in 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 arrange separately, passes through the first pipeline communication between adjacent two described clean unit devices; Described in each, clean unit device comprises the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand and the second tube connector that is communicated with the shock flow type gas-liquid reaction chamber of upright shock flow type gas-liquid reaction chamber, handstand; Described the second tube connector is to turn through 180 degree the tube connector at angle; Upright shock flow type gas-liquid reaction chamber, relative the second symmetrical setting in tube connector left and right in the shock flow type gas-liquid reaction chamber of handstand;
Also comprise liquid supply conduit, liquid backflow pipeline and for the liquid case of 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 convolution shape liquid jet pipe capable of circulation, and is deep into the indoor positive flow passage of shock flow type gas-liquid reaction and reverse flow passage; One end of described liquid backflow pipeline is communicated with the bottom of described the second tube connector, and the other end of described liquid backflow pipeline is communicated with described liquid case;
Each is communicated with in the first pipeline between adjacent two described clean unit devices and is also provided with ultraviolet lamp;
The end of the shock flow type gas-liquid reaction chamber of the handstand of clean unit device described in each 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 that is positioned at least significant end is also provided with gas-liquid separation chamber successively; Indoor gas-liquid separation guide plate and the gas-liquid separation membrane of being provided with of described gas-liquid separation.
2. percussion flow gas purge system as claimed in claim 1, is characterized in that,
In positive flow passage described in described shock flow type gas-liquid reaction chamber and described reverse flow passage, be equipped with modularization magnetic purifier; Described modularization magnetic purifier comprises the permanent magnet of the relative arranged distribution of many groups; Described convolution shape liquid jet tube portion is through between many group permanent magnets; Described convolution shape liquid jet pipe is provided with a plurality of spray holes that are line segment shape of offering along the length direction of pipe.
3. percussion flow gas purge system as claimed in claim 1, is characterized in that,
Described the first pipeline is the U-shaped pipeline that stands upside down or handstand turns through 180 degree the rectangle tube connector at angle;
Described the second tube connector is upright U-shaped pipeline 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 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 preposition filter pipe, described preposition filter pipe is positioned at the front end of the most preposition clean unit device and the shock flow type gas-liquid reaction chamber upright with this is communicated with; On described preposition filter pipe, be 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 chamber.
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 has a plurality of plicated layers along horizontal plane laying and surface.
7. percussion flow gas purge system as claimed in claim 4, is characterized in that,
The clean unit device that is 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,
The top that is used 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.
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| CN201410366353.3A CN104128059B (en) | 2014-07-29 | 2014-07-29 | Percussion flow gas purge system |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104923060A (en) * | 2015-04-21 | 2015-09-23 | 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 |
| CN110732221A (en) * | 2019-11-19 | 2020-01-31 | 盐城市迎凯涂装设备有限公司 | coating waste gas treatment system and treatment process |
| CN111790248A (en) * | 2020-07-13 | 2020-10-20 | 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 |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104923060A (en) * | 2015-04-21 | 2015-09-23 | 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 |
| CN110732221A (en) * | 2019-11-19 | 2020-01-31 | 盐城市迎凯涂装设备有限公司 | coating waste gas treatment system and treatment process |
| 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 |
| CN111790248A (en) * | 2020-07-13 | 2020-10-20 | 上海卓鼎模具有限公司 | Constant-temperature purification air inlet device and system thereof |
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| Publication number | Publication date |
|---|---|
| CN104128059B (en) | 2015-11-25 |
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