CN102416293A - Device and method for cleaning contaminated gases - Google Patents
Device and method for cleaning contaminated gases Download PDFInfo
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- CN102416293A CN102416293A CN2011101929628A CN201110192962A CN102416293A CN 102416293 A CN102416293 A CN 102416293A CN 2011101929628 A CN2011101929628 A CN 2011101929628A CN 201110192962 A CN201110192962 A CN 201110192962A CN 102416293 A CN102416293 A CN 102416293A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
The invention relates to a device for cleaning contaminated gases, organic vapors, odours and other etchant particles. The device is united with a device for biologically treated water for cleaning. The treated water returns to the production process to be especially used for executing special types of cleaning, wherein due to movement of vast nozzles arranged inside a vertical cleaning tower in multiple layers, huge surfaces formed by water drops and water mist are formed, which are factors for improving the liquid cleaning process and ensuring strong exhaust; along with cleaning solution adsorbing oxygen, an adsorption filter executes biological treatment, leading to capture of the contaminants absorbed by the liquid; therefore the cleaning water is purified; the contaminants decomposed by the special florae convert all the hydrocarbons into carbon dioxide and water; and when adsorption components are regenerated by the method and when cycling is restarted, the cleaning water is thickened by enzymes and the clean water is returned to a recycling tank and a cleaning system.
Description
Technical field
The present invention relates to a kind of contaminated gas that is used to clean, organic steam, the device of smell and other aggressive agent particles, it is an equipment that combines and use with the biological treatment device of rinse water (water is used for cleaning).Water after the purification turns back to processing procedure, even or discharge that it is also free from environmental pollution.The invention still further relates in the circulation of a sealing method of uniting the contaminated gas of cleaning of use with the biological treatment device of rinse water.
Therefore; The cleaning equipment that the present invention relates to is applicable to the department of many industry and agricultural, is used for eliminating the smell and the organic steam that appear at gas, and this smell is the fat digestion process in coating material production process, painting process, manufacturing works mainly; Essence and other production processes in discharge; For example, by the smell smell bad of the gas of volatile organic matter pollution, and this taste produces injurious effects to health sometimes.
Background technology
The traditional handicraft of any elimination gas pollutant relates to needs the again burner of temperature up to 600 degrees centigrade, is used for heated air at normal temperatures, the material of Air thing or volatile organic compound.In the process of gas-firing or fuel oil, produce great amount of heat usually, also produce high operation cost and a large amount of carbon dioxide, nitrogen dioxide and carbon monoxide simultaneously.
Having produced good effect for burnt gas in the well-designed burner more before, in such burner again, taken place to eliminate the reaction of all hydrocarbons, or converted thereof into carbon dioxide and water.Yet, be its shortcoming in order to obtain required temperature to the wilderness demand of the fuel (gas or oil) of high flow rate, because it causes very high operation cost.Therefore employed fuel is fossil fuel in these processes, and causing huge discharge amount of pollution, its discharge capacity is to have Duoed 10 or 20 times than the discharge capacity that the oxidation from the VOC that is eliminated causes.
These conditions are to have run counter to the regulation of the Kyoto Protocol of relevant minimizing greenhouse gas emission.
Catalyticing combustion process brings better result, and the need of the completing combustion of organic compound carry out under lower temperature, and its concentration surpasses 6000 milligrams/cubic metre, but need not to use extra fuel.
Under the situation of light concentration gas, in order to keep temperature, need corresponding more fuel to guarantee completing combustion, yet, produced a large amount of greenhouse gases (carbon dioxide) and other gas of not expecting for example nitrogen dioxide and carbon monoxide.
Be lower than in the concentration of organic compound under 3500 milligrams/cubic metre the situation; Need a considerable amount of gaseous fuels or a considerable amount of oil, the quantity that this means the carbon dioxide that its produces manys octuple than complete oxidation or the quantity that directly converts compound to carbon dioxide that carbon dioxide and water produces.
Be accompanied by a large amount of greenhouse gases that consume excessively and from these processes, produce of valuable electric power resource, make much human oppose suchlike equipment.The use of this equipment should be replaced by new equipment, and this new equipment also should use new method guaranteeing thoroughly to eliminate exhaust gas discharging, and then the restriction emission amount of carbon dioxide, has limited fuel consumption simultaneously.
The use biofilter of using at present comes the decomposing organism compound to meet the regulation of the Kyoto Protocol, yet the best weather conditions and the demand of corresponding device thereof have limited their efficient and function.In addition, they need large space, so that install and long-term decomposing organic matter matter, thereby cause building large scale system, are lower than 50mg/Nm but still can not satisfy
3The requirement of discharge capacity.
Be considered to complicated in the traditional sewage disposal that contains organic pollution, because the flocculation in the traditional handicraft process, flotation all is invalid with pouring into, and in the biology decomposition of sewage disposal system uncertain influence is arranged also.
On the other hand; For effect is the purge of gas system of characteristic; Aspect gas purification, eliminating these pollutants needs periodic cleaning to change water, makes pollutant can't reach maximum concentration, thereby influences efficient and bring counter productive because it can cause having reduced removing of saturated molecule.Therefore, though the solution of atmosphere problem is very important, the problem of the sewage of the generation that is associated with quality and quantity that need face, the once received shortcoming of this unique solutions through burning repeatedly also is very outstanding.
Summary of the invention
Technical problem to be solved by this invention just provide in the closed circulation of a rinse water with biological treatment device unite use to the device that cleans of contaminated gas and to the method for cleaning of contaminated gas.
For solving the problems of the technologies described above, the present invention adopts following technical scheme: a kind of method of in the cleaning fluid of closed circulation, uniting the contaminated gas of cleaning of biological treatment system, wherein; It comprises through centrifugal diffuser carries contaminated gas, and this diffuser evokes the gas motion of spinning when gas rises to cleaning tower, there; They receive bombarding of cleaning fluid, and wherein cleaning fluid is to be divided into the nozzle ejection that row are provided with by a large amount of reservations along cleaning module, forms the huge surface that a large amount of water droplets and water smoke constitute; This surface precipitation is on a large amount of concentric rings, and concentric ring is arranged on the inwall to stimulate and forms continuous waterfall, improves cleaning process, guarantees strong ventilation and guarantee that liquid constantly absorbs the factor of oxygen thereby constituted; Although contaminated, it also comprises a large amount of oxygen and is transported in the biological treatment tank that it is imported by central tube and it is had the distributor discharge of sealing flat hose therefrom; It close on part in the chamber of the bottom of jar or in first by mean allocation, it is movable and need not form preferred path through mesh material therefore to have transmitted the spiral that makes progress, and in mesh material, assemble a large amount of bacterial community; Wherein great majority are owing to the very high exhaust that takes place in the cleaning tower, and this also is very important, because a large amount of organic pollution that these microorganisms of nursing will cause resting on the there is converted into carbon dioxide and water; Then, the pollution level has here reduced a lot of liquid by upwards transmission, through second chamber or second portion; Wherein second portion is a sorbing material that is closed with predetermined quantity, and sorbing material can make and in its hole, stop other to pollute that its hole has comprised new bacteria flora also can change into carbon dioxide and water to organic contamination; Then; At this moment liquid is almost clean, but it is still doing ascending motion, and is directed to the 3rd chamber or third part; There; Filter fiber stops the particle of sorbing material to be taken away by water, and wherein water is turned back to nozzle through recirculation tank then by the enzyme enrichment of existing microorganism establishment; Through nozzle, it can be ejected at this in cleaning part.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower, gas moves up in cleaning tower, and the neutralizer that is sprayed by nozzle cleans gas; It comprises cleaning part, unites unit, gas access and recirculation tank of the tangent line setting of this part, and it is designed to the system of claim 1; Wherein the internal condition in module need be provided with the nozzle that vertically is arranged in delegation in a large number in the many zones in each part; These nozzles are encircled overlapping setting, these rings according to from big to small towards the order at the top of cleaning tower in the inwall setting, yet; Alternative; This device also comprises, is provided with the annular fluid separator in the bottom of device, and it comprises a plurality of cones that are divided into a plurality of parts and the concentric setting of quilt; They are set on the line, and the formation shutter separates each other.
The method that is used for purge gas, the device that it utilizes the biological treatment rinse water is characterized in that; It comprises a vertical column type jar, and this jar comprises first, and one is used for introducing the central disposed tubes that goes out spiral helicine ascending fluid with salt marsh; It is used for making that sewage imports to first; And first is filled by mesh material fully, and second portion is with the sealing of granular adsorption material, and third part has been equipped with filter fiber.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower; Wherein, It provides the quantity of the adjusting of nozzle, topology layout, and wherein nozzle is an arranged in series; Vertically be arranged on the particular department of each cleaning module, clean according to the type of gas and pollutant.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower; Wherein, It comprises the concentric circles conical ring on the inwall of each cleaning module of some ring section of the liquid that is arranged on to be gone out by nozzles spray, and cleaning tower is dark more, and the size of ring is more little.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower, wherein, it comprises the equipment as the annular fluid separator; Wherein, This separator is divided into the multistage of conical form, is arranged to delegation with one heart, is isolated from each other; Form overlapping shutter through such mode, this device is arranged to the curtain of cleaning module or in its inside.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower; Wherein, It has comprised Web materials; This mesh material is processed through the embossing polymer fiber of arch slightly, leaves after the embossing stage and adds sorptive material in the cooling procedure when still being in semi-solid material, rocks and vibrate the fiber that tangles then with formation.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower; Wherein, It optionally comprises the first of the jar that is sealed by layer; With the percentage definition of the active carbon of dynamic suspension, as the movable result of sewage that system introduces, it comprises that uniform mixing is to guarantee the fully closely contact of contaminated sewage with the adsorbent equipment quality inspection.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower wherein, is provided with the dispensed chambers of distributor so that sewage is discharged on the basis of pipeline.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower, wherein, the distributor of effluent sewerage is designed on the flat hose of pipeline.
A kind of device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower, wherein, nozzle is sprayed onto liquid the predetermined ring section of cleaning tower inwall; Receiving the influence that impacts, liquid crushing becomes a large amount of water droplets to form water smoke, and the inwall that some in them are cleaned tower absorbs; Be slipped to downwards on the ring below just being arranged on, they flock together and are deposited on the next ring there, and enter at the absorbed water droplet of impacting of each stage; Subsequently, they constantly precipitate, thereby create real waterfall; There, under the influence of the turbulent flow that evokes, a large amount of oxygen and gas and liquid mixing.
The method that is used for purge gas, it utilizes the device of biological treatment rinse water, and wherein, it comprises ring, and it has determined different speed, comprises that liquid increases it and stays the time in the cleaning tower; Increase the water droplet amount that contacts with gas greatly, and increased the ability of polluting absorption.
The method that is used for purge gas, it utilizes the device of biological treatment rinse water, wherein; It comprises the annular fluid separator, and it is separating liquid in each several part, there; Absorption reaction possibly take place, and therefore, various liquid can be cleaned simultaneously in same cleaning tower.
The method that is used for purge gas; It utilizes the device of biological treatment rinse water, wherein, and in the regenerative process of absorptive element; The form of the type of the active carbon of the suitable coupling of all some can be the biologically active of the special bacterial flora of coupling; This bacterial flora appears in the hole, and breeding under the influence of concrete a large amount of oxygen in the liquid in cleaning tower converts it into carbon dioxide and water under the condition that suitable current and seizure surfaces contaminated are decomposed.
The method that is used for purge gas, it utilizes the device of biological treatment rinse water, wherein, the formation that the form that is provided with on the absorption labyrinth of Web materials has stoped liquid effectively to catch the organic compound that appears at the there and be of value to the preferred path of microorganism development,
The method that is used for purge gas, it utilizes the device of biological treatment rinse water, wherein; Because the high oxidative capacity of water or sewage; In the processing procedure of water or sewage, cleaning tower is floated the device of washing device or can dissolving or spread the gas in the liquid as the ventilator of a fecund.
The method that is used for purge gas, it utilizes the device of biological treatment rinse water, wherein; Absorb the associating of organic cleaning of materials tower and organic sewage treatment plant (ETEO), form an independent covering device, they replenish each other; Cleaning tower is created in the oxygen of biodegradation organic principle; Biological treatment system produces cleaning fluid, and it is clean, and is to increase for the needed enzyme of the maximum that reaches cleaning efficiency.
Description of drawings
Below in conjunction with the accompanying drawing and the specific embodiment the present invention is further described:
Fig. 1 to 3 has described the profile of the device of the component devices that gets into the purge of gas system; Wherein system has united purge of gas and biological treatment device in a closed circulation of cleaning fluid; And accompanying drawing 1 has been described the vertical cleaning tower that has three cleaning modules (4); Fig. 2 has described the distributed amongst jar, and accompanying drawing 3 has been described and has been used in basic biological treatment or the device of phase I.
Fig. 4 has described the profile of the alternative device that is used in basic biological treatment or second stage.
Fig. 5 has described alternative profile that has the vertical cleaning tower of two cleaning modules (4), is to form curtain shape structure by the annular fluid separator (7) that is directly connected to biological treatment device (accompanying drawing 8) and be positioned at higher part.
Fig. 6 has described another view of the distribution tank in the accompanying drawing 2.
Fig. 7 has described another embodiment that this device in the accompanying drawing 3 can be used for basic biological treatment system.
Fig. 8 has described under the situation that sewage is tackled by annular fluid separator (7), and this device can be used for another embodiment of basic biological treatment system.
Fig. 9-11 has described the cleaning module (4) of the nozzle (5) of being furnished with one or more series.
Figure 12-14 has described the profile of cleaning module (4) of being furnished with the nozzle (5) of one or more series at the atomization process of rinse water, the part of also being furnished with relevant curtain shape ring segment (24) and appearing at its inner a large amount of waterfall (25)
Figure 15-17 has described the vertical view of cleaning module (4), and it is furnished with one or the nozzle of multi-series (5) more, and the visual solid geometry structure of being furnished with the zone of the injection stream that comprises cleaning fluid.
Figure 18 has described is furnished with one or the side view of inside of the cleaning module (4) of the circular cone ring (6) of the nozzle of multi-series (5) or series more.
Figure 19 has described is furnished with one or the more nozzle of multi-series (5) and the side view of inside of cleaning module (4) of visual solid geometry structure of being furnished with the zone of the injection stream that comprises cleaning fluid.
Figure 20 has described the side view of the inside of the visual cleaning module (4) of setting up typical a large amount of waterfalls.
Figure 21 has described the side view of the inside of the visual cleaning module (4) of setting up typical atomizing water layer (9).
Figure 22 has described the profile of the annular fluid separator (7) that exists with coniform element form that is made up of a plurality of parts.
Figure 23 has described the visual profile that the cleaning fluid of annular fluid separator (7) moves up and down.
Figure 24 emphasis is described inner distributor (15) of biological treatment device and closed flat hose (18).
The specific embodiment
The present invention includes a kind of set composite that dyes gas at vertical cleaning tower supernatant contaminate; On cleaning tower; Sprinkling water droplet (molecule) through serial connection is blown and is created multilayer cascade and fluosolids (suspension; Spray water); Be used for pollution abatement through introducing considerable liquid oxidatively effect, comprise, condensation (liquefaction) and tackle (gas componant is accumulated in the surfaces externally and internally (in pore) of solid) along with adsorption process and the absorption in the biological decomposition process of pollutant in the system of the sealing of rinse water treating apparatus (making the gas pollutant dissolving) through liquid.
This most distinctive function of system is to clean, and through using a large amount of nozzle 5, this nozzle is installed on many layers of inside of vertical cleaning tower of cleaning equipment; Allow to produce a considerable amount of water droplet and water smokes 9 with very big surface, this surface is created in the washing fluid, is deposited on many circular cone concentric circles 6; It is installed on the cleaning tower wall, is between some ring section 24 of sprayer (nozzle), has caused the formation of waterfall subsequently; Increased the time that water keeps the flotation material in cleaning tower, this is a key factor of improving purge gas, because a large amount of contact between liquid 9 and gas; And exposure for a long time, guaranteed strong favourable inflation, therefore; Cleaning fluid will be the main target of the biology conversion (decomposition) in adsorption filter to the absorption of oxygen; The setting of this filter is adjacent to washer, is used to purify cleaning fluid, keeps the least concentration of water pollutant.
The adsorbent (being used to catch the material of pollutant) that occurs with the active carbon form has caused when it turns back to recycling can the elimination of pollutant in the cleaning fluid.
The organic pollution that from gas, removes is used to feed special bacterium; And through they decomposition; And all hydrocarbons are changed into carbon dioxide and water; Thereby the adsorbate of regenerating (active carbon) can constantly absorb the pollutant by the cleaning fluid supply to such an extent as to they are remained under the good condition it always, then clean water is turned back to circulating tank; Circulating tank often has the concentration of lower pollutant; In order to guarantee the maximum availability of cleaning process in this method, provide a large amount of oxygen composition in the cleaning process in recirculated water, be used for guaranteeing for bacterium in order to breathe the maximum availability of requisite oxygen in biodegradation process.
Cleaning tower combines synchronously, and the purification and the oxidation in water and the sewage of the air of generation become a perfect solution; In order to destroy contaminants from gas; Comprise solid, liquid and gaseous state organic products reach through transferring to them the smell in the rinse water, and this solution is in the closed circulation; It is constantly handled through biofilter; This filter has biological decomposition function, can organic principle be changed into carbon dioxide and water, and removes the non-organic principle of outside.
On the contrary; Thermal oxide and common cleaning integrated system according to the present invention can be realized real gratifying result; Make the organic pollution of removing in the gas in each stage up to 97% (90 percent); The operation cost of eliminating undesired material is also very low, and this constitutes, and excitation is implemented and the strong motivation of operation native system.
According to solution of the present invention; A kind of biological treatment system that the present invention includes; The target that can reach us also promptly obtains the more cleaning and the purification of the gas of efficient; And the target of guaranteeing to remove (byproduct of purification process) sewage is effectively actual in processing procedure, in biological treatment system, will use special method.
Be used for the cleaning tower (Fig. 1 and 5) of the oxidation of purge gas and cleaning fluid, it is characterized in that, it has many nozzles 5 of arranging with the series connection form; Under this mode, in order to make that gas can be through 24 layers of all ring sections, wherein ring section layer promptly is the place that spray liquid takes place; Capacity and ability based on cleaning tower; Each tandem compound comprises one group of 10 nozzle, and they are in order to guarantee the uniform concentration of water droplet, and they are placed on same plane uniformly.For reach maximum validity (interface (contact-making surface of gas and liquid) is sympathized and is considered to be the mixed coefficint of water environment and gas (perhaps air), and gas or air by the maximum absorption of atomizing of liquids; And minimum friction loss, should carry out with 15 and 45 degrees centigrade angle owing to the saving and the sprinkling of energy, consider cost/profit ratio; Best angle is 35 degrees centigrade, and the angle of pipeline delivery nozzles should be identical with the angle of atomized spray or approximate, sprays in order to avoid pipeline interception frequency spectrum; The ring 6 also by with successively decrease the order top (Figure 18,20 and 21) that between the reflecting point of two atomized liquids, always reaches cleaning tower connected in series, the minimizing on its gas velocity that is used for confirming to flow through; Based on advantage,, upwards lift and remain in the suspended state through loading small-sized and light-duty water droplet from the lower floor's (sphere) that moves up with higher speed; The water droplet that produces in the intermediate layer of cleaning tower remains on average speed, and the volume of the little water droplet of tackling by atomizing is bigger, heavier; At cleaning tower top speed lower (Figure 21), ring 6 or lateral direction element that water droplet is sprayed in these interceptions are very important, because they confirm and the interior speed of differentiation cleaning tower; It has increased the suspension amount to a great extent and has descended, and helps to increase the absorption of oxygen and gas, the influence that is recycled; Because contact-making surface is big, caused producing numerous decline waterfalls 25, they drop on the wall of cleaning tower; Drop to next ring, they are collected and further drop to lower ring there, further; Add every layer spray and drip and create (Figure 20) real waterfall, wherein, in the decline process owing to water droplet and the influence of dripping the turbulent flow that the basis of the cleaning tower of beating produces; A large amount of oxygen, gas and circulation of fluid connect mutually, accomplish in order to carry out biological treatment conditions needed subsequently, especially when organic product for example the smell etc. of solvent, infiltration from fat; Feather, the pollutant that the decomposable process of blood and material produces is removed.
And along with the longitudinal structure of serial nozzle and the multistage cleaning technique (Fig. 1) of lateral loops permission application, a plurality of spheroids that perhaps are divided into have constituted the notable feature that the utilization in same cleaning tower (Fig. 5) is cleaned.
According to designing as follows, this equipment comprises the cone that is divided into a plurality of parts 8 of concentric arrangement, and is co-linear with one another as the device (Figure 22 and 23) of circulation separator 7; Make spheroid away from each other through creating overlapping shutter, and can make gas flow to the top, still from the spheroid bottom; Current can't be reduced to the spheroid bottom from the spheroid top; Because it separates into independent parts with neutralising fluid, because in the inside of same cleaning tower, differing absorption and reaction appear in multiple cleaning fluid cognition.Therefore; In first spheroid, can use acidic cleaning solution to carry out cleaning, the alkalies that cleans usefulness uses in second stage, even in the 3rd ball, has no under the interactional possibility; Utilize the minimizing of the cleaning fluid in the oxidation liquid; The demand of careful observation action flowed in the different jars (Fig. 8) in order to the guiding fluid when it provided separator interception fluid, to such an extent as to they can return through the suitable nozzle 5 that cleans specific spheroid.
Continuous purification water system in the purging system; Its objective is the elimination organic matter; And in order to prevent increasing of the solvent strength that causes saturated situation; Prevent promptly that also organic concentration from reaching peak and prevent that the water on the cleaning fluid from having lost a certain specific compound dissolution characteristics, thereby limit, even eliminated the ability of the continuous absorption of contaminants of cleaning tower.
The characteristic of the cleaning of this and biological agent combination and operation can cause guaranteeing the advantage of destroy contaminants from gas; Eliminate the pollutant in the gas with the supply of guaranteeing a considerable amount of oxygen and with the pattern of fixing and sealing; The realization of guaranteeing function is conveying continuously and the effective sewage disposal system subsequently through cleaning fluid; In sewerage, be decomposed as the pollutant of the nutritional labeling of microorganism and change into carbon dioxide and water, water is cleaned and is prepared to absorb effectively new organic products once more.
Continuous rinse water forms a loop, wherein caused continuously water being pumped into processing system and cleaning tower, and the low concentration that has kept solvent and organic products, thereby satisfied the high efficiency key condition of cleaning process.
In order to improve the attraction degree of right this pollution control device of enterpriser; Because there is disposal of pollutants in process of production in their enterprise always; In order to impel enterprisers to be ready to use the equipment of these pollution abatements in process of production, the enforcement that must restriction and the cost of operation.Because following true: the heat regeneration suction of traditional absorptive element needs complex apparatus; The labour of labor; Comprise and often to remove and to change these materials; Because the cost that microorganisms reproduction needs is lower, plants a colony the mode of absorptive element through microorganism and carried out the application of reforming in this system and equipment.
Type, quality and organic concentration according to filter are classified, and its structure has multifrequency nature.Basic, vertical cylindrical tank (referring to accompanying drawing 3 and 7) has a central tube 16, is used to handle the sewage of introducing; It comprises that distributor 15 is in order to distribute the sewage of cleaning solution or bottom; And therefore the current that it can uniform distribution makes progress need not produce preferred path in the phase I, and wherein the phase I uses mesh material to fill; Thereby make all flow of liquid through mesh and stay the part pollutant; The remaining pollutant of interception in second chamber of being filled by carbon granule then, is placed on the 3rd chamber 22 collection and purification water at top and it is led back to recirculation tank 1; Accomplish once circulation according to this, perhaps again under the situation of high concentration, the 3rd chamber is directed to second stage 4 to it, the filter array of then need flowing through this moment.
More complicated system its objective is raising to using the continuous regeneration of biological absorption in the organic decomposable process, at this moment need utilize the multi-stage biological filter of three or more processing section.
In order to make outer surface increase to maximum; To obtain only geometric path; And the best distribution that obtains the input contraction of optimum capacity and removable powder bed, can utilize active carbon as sorbing material, because the high-absorbable and the small size property of carbon dust moment suction; It has caused it to be deposited in traditional system bottom, and on the layer of contiguous bottom, assembles.
The obstruction of the nozzle on the sewage distributor that is used for biological treatment device because this biological treatment device has carbon powder particle, therefore causes it to lose when taking place to stop up in system its suspension characteristic; At this moment utilize the smooth flexible pipe 18 of a lengthening; The one of which end has horizontal interface, and flexible pipe is set up in the following manner and installed, and it can be opened when distributing sewage; When current stop, closing, this structure can prevent that particle from arriving distributor 15.
In this case; No matter phase I or second stage; The part of the first 26 of jar is filled carbon dust; Mix when sewage injection nozzle and water jet delivery port (sprinkler) utilize compressed air guiding high energy, this mixing makes the powder in the suspension set up surface fully uniformly, and the concentration of this uniform outer surface is controlled in the scope of 5-70%.Dynamic surface does not allow in the input spheroid, to have high concentration carbon; The factor of setting up the input spheroid is to inject together linked together with the set of regulating input sewage; Wherein the sewage of input is by centrifugal unloading; So its can not set up preferential route with the reduction system in the negative effect aspect the efficient, it has increased its effectiveness.
In addition; Because the flowability of the suspension that phase I powder and sewage are set up can be changed easily; Change in this and need not go to remove or block system and its filter can reach, the second portion 27 of jar, its effect is to accomplish first and prevent that powder from rising to next part; Guarantee to form huge labyrinth by the outer surface that mesh material 19 is processed; Wherein the early stage sewage handled of phase I must flow through it and stay carbon powder particle and pollutant, the mesh material here is made up of fiber freely, this part is filled with the mesh material that has coated active carbon; Its activated carbon particles stops in the labyrinth, and this is permanent to have constituted the outer surface that makes that microorganism species effectively exposes.
Because a fact, promptly fluid closely contacts with these surfaces, has occurred the decomposition of the minimum concentrations of organic principle in the sewage.The 3rd part 28 often also is last part, though be not in all technical schemes, all to occur; It is filled by durable active carbon and forms or be made up of the mixing of adsorbate, and through this adsorbent, clean fluid is flowed through; Constituted the zone of the residue in the destroy contaminants, after this, sewage is directed to purge of gas or other stages again; These stages carry out successively, and often rely on existing pollutant kind and concentration.
For the cleaning tower of accepting a special construction, there, the liquid that band cleans is by meticulous billions of water droplet that is ground into; These are different with the processing in the legacy system, and in traditional system, they contact the longer time with gas; Thereby through absorption, pollutant is transferred to biofilter, there; All impossible preferential routes occur, if not through cleaning effectively, gas be can't through this system (for example; Packed column), guarantees the foundation in numerous zones of vertical structure of fluid layer and atomizing, since it allows the increase of dissolved nutrients; It has satisfied the scope for the needed physical condition of good associating between purge of gas device and the wastewater treatment plant, therefore, can set up a kind of system that in single operation, can destroy and eliminate organic pollution together.
A biofilter is through stepping filter and this systems incorporate, and it can remove insoluble material like paint, powder, and lubricating oil, oil is cleaned the refuse that tower is intercepted and captured with other.
The application of this system is very necessary, especially avoids the similar jammed and pollution problems that is used in the absorption element in the biofilter of emerged in operation as needs.Basically; It possibly comprise a distribution tank (Fig. 2) wherein, and the flotation material for example paints or dyestuff constantly overflows from the distribution tank of cleaning tower and flow to distribution tank, from distribution tank; It can removing or sometimes even be filtered by machinery; Yet if accomplish such function, saturated filter must be removed subsequently.
Biofilter is a kind of system of disposing of sewage of can really being used to, and this sewage has comprised a large amount of organic substances, particularly solvent.Yet, a lot of other compositions are also arranged, for example comprising feed, lubricating oil; Oil, blood, bone; Fish food etc., they all have specific smell and can in such filter, be decomposed, but it can be quite simple can be used in the filter that removes them; For example, have a single chamber, the frame for movement of its sealing comprises a kind of sorbing material of specific quantity or the place that the group that is filled in microorganism or bacterium fixing or that move assembles.This is a characteristic relevant with the microorganism demand.Contaminated fluid this structure of flowing through; The jar of the filling that its employing sorbing material and/or filler carry out; After staying organic contamination, decomposed by microorganism then, wherein microorganism occurs with the form of multigroup group; And it provides nutrient and changes into carbon dioxide and water to them, the sorbing material of regenerating simultaneously for these compounds.Most critical be this structure of guaranteeing this element, wherein, this element can make the preferential route that fluid can not occur overrunning, and has prevented that therefore the gathering of pollutant from contacting with surperficial, and the absorption of filtering material.
The mesh material 19 that uses can be processed by the embossing fiber that omits arch, for example from following material: still be in semisolid PP, PF; PVC and polyamide after these materials leave the embossing stage, add the for example powder of carbon or active carbon of sorptive material in cooling procedure; Coat these powder then; Again, the fiber that rocks and vibrate entanglement is to form real labyrinth, and this is the ideal structure that guarantees best contact between sewage and the microorganism.This structure that the fiber that is coated by active carbon is processed is the place of desirable accumulation microorganism, is noted that carbon absorbs the inboard of its molecular structure with organic compound, and gap that the there is huge or pore have produced the attraction that stops and absorb these compounds.
The characteristic of the absorptive element of using among this paper is; It has macrovoid and size above 3 microns; The biologically active that constitutes key feature of the present invention does not allow the state of reaching capacity, because it has kept the reproduced state that continues through microorganism, the existence of macrovoid and appropriate size can offer the more surface of microorganism and regional than the outer surface of general absorption molecule; Therefore, allow huge micropopulation to accumulate in the limited surface of adsorbate.
For fear of the appearance of this situation, suppressed to close on the decomposition reaction of the microorganism of sewage inlet when organic substrate concentration is too high, such inlet should be installed in different layers.
Biologically active comprises the decomposition reaction that the microorganism of living in groups in a large number on sorbing material causes, this has caused setting up the enzyme of enrichment cleaning fluid, has therefore improved the efficient that restarts circulation time purge gas process.
By this method; In cleaning tower, sewage is imported in recirculation and the atomizing processing again, and at this moment sewage removes new pollutant at any time with form cleaning, enrichment; Simultaneously; Prevent the increase of the concentration of ordinary dissolution in the recirculation tank of sewage, this concentration invariably accompany with the operation of good water quality with the maintenance, use, wearing and tearing, the operating cost that reduce pump and eliminated the frequent expense that needs to change cleaning fluid, these are key factors of the possibility utilized of restriction legacy system.
Can improve the efficient of biological treatment system through dissolving a large amount of oxygen itself; Through creating to the enzyme of significant contribution is arranged for the generation of water in the cleaning recycled; Thereby fundamentally limited the concentration of volatile organic component, these methods originally are used for the mediation system of the cleaning of gas all by in design; This The Application of Technology has been guaranteed the productivity, high efficiency and the minimum operation cost that continue.
The purge of gas device comprises by many overlapping parts; Form a cylindrical orthogonal cleaning tower (Fig. 1 and 5); Its basis is recirculation water tank and storage cistern 1, and they have a flow element 2, and it has limited a surface; Through this surface, the contaminated liquids of storage is transferred to distribution tank (Fig. 2) before.The gas input block that tangent line is placed comprises a centrifugal diffuser 3, and when rising cleaning tower, this centrifugal diffuser evokes the gas of screw.In purge of gas module 4, the nozzle 5 of one or more different series is arranged, they through such mode install can with the circumferential ring overlaid of the guillotine of atomizing fluids.Selective ring-type current separator 7 comprises a plurality of bullets 8, and it is divided into the concentric a plurality of parts away from each other of level, and this helps the formation of eclipsed form shutter, and it tackles fluid 9 from cleaning module 4.Whole device is closed by a decline brake 10, and this decline brake comprises a plurality of parallel and vertical with cleaning tower ribs.
Pans as distribution tank (Fig. 2) are to be placed between distribution tank 1 and the biological treatment tank (Fig. 3 or Fig. 4), and it is provided with a cylindrical tank, and it comprises a lot of containers and first; Wherein first removes the flotation material in the phase I; Simultaneously, it also is provided with the flow element 12 of a limiting surface, through this element; Fluid flows to main distribution tank 13 or flows to second portion; Wherein in second stage, the legacy of the floating layer of the cleaning fluid in the second portion is removed, and this removes through sucking pump 14 and is transferred to biological treatment tank (Fig. 3 or Fig. 4).
The Sewage Biological Treatment equipment that produces in the cleaning tower (Fig. 1 or Fig. 5) consists essentially of (Fig. 3) cylindrical orthogonal jar; This jar comprises the different piece that overlaps each other together; It is provided with basic first; The sewage of distributor 15 is flowed out and flow on the top that is used for collecting the inlet of the passage that is provided with from the center, and at the distributor place, the end of pipeline 16 is flat hose forms 18; The mesh 19 of the inside of sewage through being arranged on this part is assigned to the bottom of cylindrical tank uniformly, and it has evoked the screw of ascending fluid when not obtaining the information of preferred path simultaneously.Through second chamber 20 or by the second portion of the sorbing material sealing of scheduled volume, from before the effluent stream that flows into of chamber to the 3rd chamber.The 3rd chamber 22 or the third part that has been equipped with filter fiber be configured to catch the particle of adsorbent equipment, and they are likely is brought by the sewage in the last stage remittance of this device implementation.
In outlet, be stored in the recirculation tank from the clean waste water of biological effluent treatment system, from it is pumped into the nozzle 5 of vertical cleaning tower here, begins another new cleaning and wastewater treatment and circulate.
Topology layout in example proposed by the invention, it is primary can carrying out construction, because this equipment has modular construction; Its a plurality of parts, sections, department and above-mentioned field need merge or carry out as required; This need depend on the type that is removed material when cleaning, the concentration of quantity and/or pollution, and after biological treatment takes place; When various variants use, to obtain best association system possibility.Can find out clearly that from top introduction the present invention has lot of advantages, it obtains an advantage from the following fact: the processing to biological sludge is avoided in its operating process, simultaneously; Prevent friction; Jammed and the sensitiveness to pollute changing the more important thing is that it can not discharge excessive carbon monoxide; Nitrogen dioxide and carbon dioxide, the carbonic acid that produces in its implementation process also are easy to be neutralized.
The technology of introducing above the present invention is not limited to of giving an example; But it comprises the whole gas purge system of catching organic compound; Comprise that simultaneously elimination is in biology decomposition and purification process; And the pollution that produces in the process of enrichment rinse water, it also comprises the application of characteristic in follow-up method among the present invention.
The applicant has the right to keep and also has other creative characteristics, its literal of the present invention and accompanying drawing describe still be not included in below content.
Claims (17)
1. the method for the contaminated gas of cleaning of an associating biological treatment system in the cleaning fluid of closed circulation, wherein, it comprises through centrifugal diffuser (3) carries contaminated gas; This diffuser evokes the gas motion of spinning when gas rises to cleaning tower, there, they receive bombarding of cleaning fluid; Wherein cleaning fluid is to be divided into nozzle (5) ejection that row are provided with by a large amount of reservations along cleaning module (4), forms the huge surface that a large amount of water droplets and water smoke (9) constitute, and this surface precipitation is on a large amount of concentric ring (6); Concentric ring is arranged on the inwall to stimulate and forms continuous waterfall (25), improves cleaning process, guarantees strong ventilation and guarantee that liquid constantly absorbs the factor of oxygen, although contaminated thereby constituted; But it also comprises a large amount of oxygen and is transported in the biological treatment tank, and the distributor (15) that it is imported by central tube (16) and its is had sealing flat hose (18) is therefrom discharged, it close on part in the chamber of the bottom of jar or in first by mean allocation; Therefore transmitted the spiral activity that makes progress and need not form preferred path through mesh material, in mesh material, assemble a large amount of bacterial community, wherein great majority are owing to the very high exhaust that takes place in the cleaning tower; This also is very important, because a large amount of organic pollution that these microorganisms of nursing will cause resting on the there is converted into carbon dioxide and water, then; The pollution level has here reduced a lot of liquid by upwards transmission, and through second chamber (20) or second portion, wherein second portion is a sorbing material that is closed with predetermined quantity; Sorbing material can make and in its hole, stop other pollution; Its hole has comprised new bacteria flora also can change into carbon dioxide and water to organic contamination, and then, liquid at this moment is almost clean; But it is still doing ascending motion; And be directed to the 3rd chamber or third part, there, filter fiber (23) stops the particle of sorbing material to be taken away by water; Wherein water is by the enzyme enrichment of existing microorganism establishment; Turn back to nozzle through recirculation tank then, through nozzle, it can be ejected at this in cleaning part.
2. device that is used to clean contaminated gas that comprises at least one vertical cylinder cleaning tower, gas moves up in cleaning tower, by the neutralizer of nozzle (5) ejection gas is cleaned; It comprises cleaning part, unites unit, gas access and recirculation tank of the tangent line setting of this part, and it is designed to the system of claim 1; Wherein the internal condition in module (4) need be provided with the nozzle (5) that vertically is arranged in delegation in a large number in the many zones in each part; These nozzles are encircled (6) overlapping setting, these rings according to from big to small towards the order at the top of cleaning tower in the inwall setting, yet; Alternative; This device also comprises, is provided with annular fluid separator (7) in the bottom of device, and it comprises a plurality of cones (8) that are divided into a plurality of parts and the concentric setting of quilt; They are set on the line, and the formation shutter separates each other.
3. the method that is used for purge gas as claimed in claim 1, the device that it utilizes the biological treatment rinse water is characterized in that; It comprises a vertical column type jar, and this jar comprises first, and one is used for introducing the central disposed tubes (16) that goes out spiral helicine ascending fluid with salt marsh; It is used for making that sewage imports to first; And first is filled by mesh material fully, and second portion is with the sealing of granular adsorption material, and third part has been equipped with filter fiber.
4. device according to claim 1 and 2, wherein, it provides the quantity of the adjusting of nozzle (5); Topology layout; Wherein nozzle is an arranged in series, vertically is arranged on the particular department of each cleaning module (4), cleans according to the type of gas and pollutant.
5. device according to claim 1 and 2, wherein, it comprises the concentric circles conical ring (6) on the inwall of each cleaning module (4) of some the ring section (4) that is arranged on the liquid that sprayed by nozzle (5), and cleaning tower is dark more, and the size of ring is more little.
6. according to claim 1 or 2 or 4 or 5 described devices, wherein, it comprises the equipment as annular fluid separator (7); Wherein, This separator is divided into the multistage of circular cone (8) form, is arranged to delegation with one heart, is isolated from each other; Form overlapping shutter through such mode, this device is arranged to the curtain of cleaning module (4) or in its inside.
7. according to claim 1 or 3 described devices; Wherein, It has comprised Web materials (19); This mesh material is processed through the embossing polymer fiber of arch slightly, leaves after the embossing stage and adds sorptive material in the cooling procedure when still being in semi-solid material, rocks and vibrate the fiber that tangles then with formation.
8. according to claim 1 or 3 described devices; Wherein, It optionally comprises the first (26) of the jar that is sealed by layer; With the percentage definition of the active carbon of dynamic suspension, as the movable result of sewage that system introduces, it comprises that uniform mixing is to guarantee the fully closely contact of contaminated sewage with the adsorbent equipment quality inspection.
9. according to claim 1 or 3 described devices, wherein, the dispensed chambers of distributor (15) so that sewage is discharged is set on the basis of pipeline (16).
10. according to claim 1 or 3 or 9 described devices, wherein, the distributor of effluent sewerage (15) is designed on the flat hose (18) of pipeline (16).
11. according to claim 1 or 2 or 4 or 5 described devices, wherein, nozzle (5) is sprayed onto liquid the predetermined ring section (24) of cleaning tower inwall; Receiving the influence that impacts, liquid crushing becomes a large amount of water droplets to form water smoke, and the inwall that some in them are cleaned tower absorbs; Be slipped to downwards on the ring (6) below just being arranged on, they flock together and are deposited on the next ring there, and enter at the absorbed water droplet of impacting of each stage; Subsequently, they constantly precipitate, thereby create real waterfall; There, under the influence of the turbulent flow that evokes, a large amount of oxygen and gas and liquid mixing.
12. according to claim 1 or 2 or 5 or 11 described methods, wherein, it comprises ring (6), it has determined different speed, comprises that liquid increases it and stays the time in the cleaning tower; Increase the water droplet amount that contacts with gas greatly, and increased the ability of polluting absorption.
13. according to claim 1 or 6 described methods, wherein, it comprises annular fluid separator (7), it is separating liquid in each several part, there, absorption reaction possibly take place, and therefore, various liquid can be cleaned simultaneously in same cleaning tower.
14. method according to claim 1, wherein, at absorptive element (19; 20,26,27; 28) in the regenerative process, the form of the type of the active carbon of the suitable coupling of all some can be the biologically active of the special bacterial flora of coupling, and this bacterial flora appears in the hole; Breeding under the influence of concrete a large amount of oxygen in the liquid in cleaning tower converts it into carbon dioxide and water under the condition that suitable current and seizure surfaces contaminated are decomposed.
15. according to claim 1 or 2 or 6 described methods, wherein, the formation that the form that is provided with on the absorption labyrinth of Web materials (19) has stoped liquid effectively to catch the organic compound that appears at the there and be of value to the preferred path of microorganism development.
16. according to claim 1 or 2 or 6 described devices, wherein, because the high oxidative capacity of water or sewage, in the processing procedure of water or sewage, cleaning tower is floated the device of washing device or can dissolving or spread the gas in the liquid as the ventilator of a fecund.
17., wherein, absorb the associating of organic cleaning of materials tower and organic sewage treatment plant (ETEO) according to the described method of the 1-16 of claim; Form an independent covering device; They replenish each other, and cleaning tower is created in the oxygen of biodegradation organic principle, and biological treatment system produces cleaning fluid; It is clean, and is to increase for the needed enzyme of the maximum that reaches cleaning efficiency.
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CN2011101929628A CN102416293A (en) | 2011-07-11 | 2011-07-11 | Device and method for cleaning contaminated gases |
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CN2011101929628A CN102416293A (en) | 2011-07-11 | 2011-07-11 | Device and method for cleaning contaminated gases |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106525911A (en) * | 2016-12-08 | 2017-03-22 | 黎明职业大学 | Electrical conductivity electrode convenient to rinse |
CN109814549A (en) * | 2018-12-29 | 2019-05-28 | 北京英视睿达科技有限公司 | A kind of methods, devices and systems of determining pollution source position |
CN111227204A (en) * | 2017-05-14 | 2020-06-05 | 聂世林 | Apple piece making devices's washing case |
CN113490538A (en) * | 2019-03-11 | 2021-10-08 | 卡里姆·萨利普尔 | Contaminant trap and purifier |
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2011
- 2011-07-11 CN CN2011101929628A patent/CN102416293A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106525911A (en) * | 2016-12-08 | 2017-03-22 | 黎明职业大学 | Electrical conductivity electrode convenient to rinse |
CN106525911B (en) * | 2016-12-08 | 2023-04-14 | 黎明职业大学 | Conductivity electrode convenient to clean |
CN111227204A (en) * | 2017-05-14 | 2020-06-05 | 聂世林 | Apple piece making devices's washing case |
CN109814549A (en) * | 2018-12-29 | 2019-05-28 | 北京英视睿达科技有限公司 | A kind of methods, devices and systems of determining pollution source position |
CN109814549B (en) * | 2018-12-29 | 2023-11-10 | 北京英视睿达科技股份有限公司 | Method, device and system for determining pollution source position |
CN113490538A (en) * | 2019-03-11 | 2021-10-08 | 卡里姆·萨利普尔 | Contaminant trap and purifier |
CN113490538B (en) * | 2019-03-11 | 2023-11-28 | 卡里姆·萨利普尔 | Pollutant trap and purifier |
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Application publication date: 20120418 |