CN2597063Y - Air pollution purifying equipment - Google Patents
Air pollution purifying equipment Download PDFInfo
- Publication number
- CN2597063Y CN2597063Y CNU03214931XU CN03214931U CN2597063Y CN 2597063 Y CN2597063 Y CN 2597063Y CN U03214931X U CNU03214931X U CN U03214931XU CN 03214931 U CN03214931 U CN 03214931U CN 2597063 Y CN2597063 Y CN 2597063Y
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- Prior art keywords
- chamber
- purification
- purification device
- communicated
- exhaust
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 238000003915 air pollution Methods 0.000 title abstract description 5
- 238000000746 purification Methods 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 30
- 238000005192 partition Methods 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 238000001556 precipitation Methods 0.000 claims abstract description 13
- 238000005507 spraying Methods 0.000 claims abstract description 7
- 239000007921 spray Substances 0.000 claims abstract description 3
- 238000000926 separation method Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 239000004094 surface-active agent Substances 0.000 claims description 7
- 230000001939 inductive effect Effects 0.000 claims description 5
- 238000010992 reflux Methods 0.000 claims description 4
- 238000004062 sedimentation Methods 0.000 claims description 4
- 230000002378 acidificating effect Effects 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 3
- 239000000428 dust Substances 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000005202 decontamination Methods 0.000 abstract 4
- 230000003588 decontaminative effect Effects 0.000 abstract 4
- 230000010412 perfusion Effects 0.000 abstract 2
- 239000003517 fume Substances 0.000 abstract 1
- 231100001261 hazardous Toxicity 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 32
- 239000003570 air Substances 0.000 description 18
- 239000000126 substance Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 8
- 238000007599 discharging Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000004071 soot Substances 0.000 description 4
- 229910052925 anhydrite Inorganic materials 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Substances [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 3
- 239000004568 cement Substances 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- -1 i.e. Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002341 toxic gas Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
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- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model relates to an air pollution decontamination equipment which includes a stage purification device, a feeding device and a precipitation equipment, wherein the decontamination device and the feeding device are communicated with the precipitation equipment through pipes; the stage purification device includes an intake chamber, a decontamination chamber and an exhaust room which are communicated with the purification device; a multistage mesh partition and perfusion tube are arranged inside the decontamination chamber, a spraying nozzle is opened on the perfusion tube to spray liquid to the mesh partition. The precipitation equipment includes a reaction tank, a circumfluence tank and a filter tank which are communicated with the precipitation equipment. The utility model can actually and effectively remove the fume, dust and other hazardous matters and produce usable products, thus realizing the effect of changing wastes into valuables.
Description
One, the technical field
The utility model relates to a purifying device for eliminating air pollution.
Second, background Art
In modern society, industrial and mining enterprises and people use a great deal of combustible and heating furnace bodies in life, and CO contained in exhaust gas of the furnace bodies2、SO2、H2S, smoke and dust and various other harmful substances cause atmospheric pollution. Traditional gas-liquid contact purification equipment, such as water film dust removal equipment, sieve plate tower and the like, can only remove dust in flue gas, and has no effect on toxic gas and dust with micron-sized particle size in the flue gas, and the traditional gas-liquid contact purification equipment can not remove the toxic gas and the dust with micron-sized particle sizeHarmful substances cause harm to the ambient air, so that the air is polluted and forms acid rain. In order to further remove the pollutants, a common method is to add special equipment for purification, such as electric dust removal equipment, lime magnesium oxide desulfurization equipment and the like, and the equipment has high manufacturing cost and running cost, so that the cost for treating the atmospheric pollution is increased, and the popularization and application of the equipment are also limited.
Third, the invention
The utility model aims at providing an atmosphere pollution clarification plant of high efficiency, low cost.
The utility model relates to an atmosphere pollution purifying device, which comprises a multi-stage purifying device, a feeding device and a precipitation separating device, wherein the purifying device and the feeding device are communicated with the precipitation separating device through pipelines; the multi-stage purification device comprises an air inlet chamber, a purification chamber and an exhaust chamber which are communicated in sequence, wherein an air inlet is formed in the air inlet chamber, a mesh-shaped partition plate and a liquid conveying pipe are arranged in the purification chamber, a spraying opening is formed in the liquid conveying pipe to spray liquid to the mesh-shaped partition plate, an exhaust opening is formed in the exhaust chamber, and an air inducing device is arranged in the exhaust chamber.
The purification chamber is divided into a plurality of multi-stage purification areas which are communicated with each other by a plurality of mesh-shaped clapboards.
The cross-sectional areas of the air inlet chamber and the air outlet chamber are smaller than the cross-sectional area of the purification chamber.
The liquid with acidic, alkaline or neutral surfactant is conveyed in the transfusion tube.
The air inducing device is an exhaust fan driven by a stepless speed regulating motor.
The sedimentation separation device comprises a reaction tank, a reflow tank and a filter tank which are communicated in sequence, the purification device and the feeding device are connected to the reaction tank through pipelines, and the reaction tank, the reflow tank and the filter tank are all provided with discharge ports.
The filtering tank of the precipitation separation device is communicated with the liquid conveying pipe of the purification device through a circulating pipeline, and a water pump is arranged in the circulating pipeline.
The utility model provides an atmosphere pollution clarification plant, its design has stronger scientificity: first, according to raoult's law, the solubility of a gas in water is proportional to its partial pressure and inversely proportional to its temperature. Therefore, in order to make the harmful gas absorbed and purified by water in the liquid and gas purifying equipment, it is most effective to increase the gas pressure of the gas and reduce the temperature of the gas and liquid. Secondly, depending on the physicochemical characteristics of the soot, to convert the soot from a gaseous state to a liquid state, one must destroy the surface chemistry of the soot particles, and the water particle size must match the particle size of the soot particles to provide an "affinity" for the surface tension. Based on the basic thought and scientific basis, the multi-stage purification device is designed in the equipment, the smooth circulation of gas is ensured by reasonably arranging the cross-sectional area of the air chamber and the air inducing device, and the liquid with the surfactant is sprayed by the multi-layer mesh-shaped partition plates to form a water film, so that harmful substances in the atmosphere are settled to the maximum extent. Then, the sediment reacts with the chemical substances fed by the feeding device in the reaction tank to form a product which can be utilized, so that the effect of changing waste into valuable is achieved. In a word, the device has compact and simple structure, stable and reliable quality, economical and practical manufacturing cost and running cost, convenient use and capability of practically and effectively removing smoke, dust and harmful substances, and practical application shows that the effect of the device is superior to that of the existing device.
Description of the drawings
The present invention will be described in further detail with reference to the accompanying drawings and examples.
Fig. 1 is a schematic structural view of an atmospheric pollution purifying apparatus.
Fig. 2 is an enlarged view of a portion a in fig. 1.
Fig. 3 is a right side view of fig. 2. (showing the structure of the mesh-like separator)
Fig. 4 is a sectional view taken along the direction B-B in fig. 1 (showing the structure of the flow cell).
Fifth, detailed description of the invention
As shown in fig. 1, the air pollution purifying apparatus includes a multi-stage purifying device, a feeding device and a precipitation separation device.
The multi-stage purification device comprises an air inlet chamber 1, a purification chamber 2 and an exhaust chamber which are communicated in sequence, wherein the cross-sectional areas of the air inlet chamber 1 and the exhaust chamber are smaller than that of the purification chamber 2. The intake chamber 1 is provided with an intake port 1 a.
As shown in fig. 2 and 3, the purification chamber 2 is partitioned by mesh-like partitions 3a, 3b, 3c into a plurality of purification zones 4a, 4b, 4c, 4d which are connected in series. The mesh-shaped partition plates 3a, 3b and 3c are arranged in the limiting grooves 12a and 12b on the upper wall and the lower wall of the purifying chamber 2, and can be disassembled, replaced and cleaned. The mesh on the baffle plate can be selected from 6 meshes to 120 meshes according to the property and the flow rate of the polluted gas to be treated. The liquid transport tubes 5a, 5b, 5c are provided at the upper part of the clean room 2, near the mesh-like partition plates 3a, 3b, 3c, and transport a liquid containing an acidic, basic or neutral surfactant. The liquid conveying pipe is provided with a spraying port 6 for spraying liquid to the mesh-shaped partition plate, and the surfactant can promote the liquid to quickly form a water film on the mesh-shaped partition plate. The spraying of different concentrations, viscosities and flow rates can be formed by changing the aperture of the spraying port 6. The lower part of the purification zone 4d is provided with a liquid discharge 10a, which discharge 10a is connected to the sedimentation separation device by means of a pipe 11.
In order to better realize the functions of induced air and exhaust and the convenience in manufacturing and installation, the exhaust chamber is formed by connecting two mutually communicated parts: a transition zone 7a communicating with the purification zone 4d of the purification chamber 2 and an induced air discharge zone 7 b. The induced air discharging area 7b is provided with an exhaust port 8, an exhaust fan 9 is arranged in the induced air discharging area, and the exhaust fan 9 is driven by a stepless speed regulating motor. The stepless speed regulating motor has the advantage that the rotation speed can be automatically regulated according to the requirement of exhaust.
The working process of the multistage purification device is as follows: (1) the polluting gases to be purified, such as the hot gases emitted by various boilers, are generally charged with CO, CO2、SO2、H2S, smoke dust and various other harmful substances, wherein the gas enters the gas inlet chamber 1 through the gas inlet 1a, slowly flows and is cooled and then enters the purifying chamber 2, and the gas is purifiedThe cross-sectional area of the gasification chamber 2 is larger than that of the gas inlet chamber 1, and the flow speed of the gas is further slowed down.
(2) The gas entering the purifying chamber 2 is filtered and cooled by a mesh-shaped partition plate 3a in a purifying area 4a, coarse and heavy particles are firstly settled, and the adhered surfactant falls to the bottom of the purifying chamber 2; the gas then enters the cleaning zone 4b and passes through the mesh-like partition 3b, the surface active substance continues to adhere to the finer particles in the gas and falls to the bottom of the cleaning chamber 2, at which point most of the dust and dirt has been removed. In the purification zone 4c, the temperature of the gas can be controlled below 60 ℃ by controlling the cooling circulation rateThe body is further filtered and settled by a mesh-shaped partition plate 3 c. At the same time, CO in the gas2、SO2、SO3、H2S, and the like, and reacts with sprayed water:
when the gas enters the purification area 4d, the gas does not contain dust and harmful substances, and is completely purified, so that the emission requirement is met. The liquid which descends to the bottom of the clean room 2 in the above process carries dust, dirt and reaction products such as H2CO3、H2SO4、H2SO48H, from the liquid discharge port 10a through the pipe 11 into the precipitation separation device.
(3) Due to the multi-stage continuous process through the purification chamber 2, the gas flow rate has dropped considerably to 1/2 of the original flow rate and has begun to block the gas flow in the gas inlet chamber 1. At this time, since the cross-sectional area of the exhaust chamber transition area 7a is smaller than that of the purification chamber 2, the velocity of the gas can be increased, and the gas enters the induced air discharge area 7b and is discharged from the exhaust port 8. Because the exhaust fan 9 is driven by the stepless speed regulating motor and arranged in the induced air discharging area, the flow velocity of the gas is promoted and compensated, and the uniform and smooth discharging process is ensured. The harmful humic substances in the discharged gas are greatly reduced, and the damage degree to the equipment is greatly reduced when the temperature is reduced to below 50 ℃.
The charging device is used for providing chemical reactants for treatment, CaO and water are respectively added into a charging pool 14 from material ports 13a and 13b, and Ca (OH) is generated through pool reaction2，Ca(OH)2Is fed to the precipitation separation unit via line 15.
The sedimentation separation device comprises a reaction tank 16, a reflux tank 17 and a filter tank 18 which are communicated in turn. The liquid from the purification device and Ca (OH) from the feeding device2After filtration through the screen 19, the reaction is carried out in the reaction tank 16:
CaCO as a product thereof3、CaSO4And is discharged from the discharge port 20 a. The liquid is further precipitated by the reflux pool 17, and the precipitate is discharged from the discharge port 20 b. The structure of the flow cell 17 is shown in fig. 4, and is separated into curved groove shape by a baffle plate to make the liquid flow slowly and precipitate the impurities. The liquid from the rotary flow tank 17 passes through the filter tank 18, and the impurities in the tank are discharged from a discharge port 20 c. The liquid flowing out of the filter tank 18 passes through waterThe pump 21 and the circulation duct 22 can circulate the infusion tubes 5a, 5b, 5 c.
CaCO discharged from the discharge ports 20a, 20b, and 20c3、CaSO4Can be reused in industry: CaSO4, i.e., gypsum or calcined gypsum, is useful as a filler for paper, white paint, buffing powder, gas drying agent, etc., and is useful in metallurgy and agriculture; CaCO3I.e. calcium carbonate (limestone), for the manufacture of cement, ceramics, lime, chalk, pigments, fillers, neutralizers, polishes, etc., and, in addition, is the simplest, practical and convenientThe cement is used as a cement filler for building and road construction. The dual functions of waste gas treatment and waste material conversion are achieved, and the problem of secondary pollution is completely solved.
The equipment is provided with an electric control cabinet which controls the operation of the stepless speed regulating motor, the water pump motor and the stirrers 23a, 23b and 23 c.
Claims (7)
1. Atmosphere pollution clarification plant, its characterized in that: the device comprises a multi-stage purification device, a feeding device and a precipitation separation device, wherein the purification device and the feeding device are communicated with the precipitation separation device through pipelines; the multi-stage purification device comprises an air inlet chamber, a purification chamber and an exhaust chamber which are communicated in sequence, wherein an air inlet is formed in the air inlet chamber, a mesh-shaped partition plate and a liquid conveying pipe are arranged in the purification chamber, a spraying opening is formed in the liquid conveying pipe to spray liquid to the mesh-shaped partition plate, an exhaust opening is formed in the exhaust chamber, and an air inducing device is arranged in the exhaust chamber.
2. The atmospheric pollution purification device according to claim 1, characterized in that: the purification chamber is divided into a plurality of multi-stage purification areas which are communicated with each other by a plurality of mesh-shaped clapboards.
3. The atmospheric pollution purification device according to claim 1, characterized in that: the cross-sectional areas of the air inlet chamber and the air outlet chamber are smaller than the cross-sectional area of the purification chamber.
4. The atmospheric pollution purification device according to claim 1, characterized in that: the liquid with acidic, alkaline or neutral surfactant is conveyed in the transfusion tube.
5. The atmospheric pollution purification device according to claim 1, characterized in that: the air inducing device is an exhaust fan driven by a stepless speed regulating motor.
6. The atmospheric pollution purification device according to claim 1, characterized in that: the sedimentation separation device comprises a reaction tank, a reflux pool and a filter tank which are communicated in turn, the purification device and the feeding device are connected to the reaction tank through pipelines, and the reaction tank, the reflux pool and the filter tank are all provided with discharge ports.
7. The atmospheric pollution purification device according to claim 1, characterized in that: the filtering tank of the precipitation separation device is communicated with the liquid conveying pipe of the purification device through a circulating pipeline, and a water pump is arranged in the circulating pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU03214931XU CN2597063Y (en) | 2003-01-27 | 2003-01-27 | Air pollution purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU03214931XU CN2597063Y (en) | 2003-01-27 | 2003-01-27 | Air pollution purifying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2597063Y true CN2597063Y (en) | 2004-01-07 |
Family
ID=34159907
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU03214931XU Expired - Fee Related CN2597063Y (en) | 2003-01-27 | 2003-01-27 | Air pollution purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2597063Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474861A (en) * | 2014-11-13 | 2015-04-01 | 中国石油化工股份有限公司 | Skid-mounted liquid sulfur tank tail gas purifying oxidation absorbing apparatus |
| CN113082972A (en) * | 2021-02-23 | 2021-07-09 | 农业农村部环境保护科研监测所 | Pulse plasma composite multistage water film deodorization device and deodorization method for breeding house |
-
2003
- 2003-01-27 CN CNU03214931XU patent/CN2597063Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474861A (en) * | 2014-11-13 | 2015-04-01 | 中国石油化工股份有限公司 | Skid-mounted liquid sulfur tank tail gas purifying oxidation absorbing apparatus |
| CN113082972A (en) * | 2021-02-23 | 2021-07-09 | 农业农村部环境保护科研监测所 | Pulse plasma composite multistage water film deodorization device and deodorization method for breeding house |
| CN113082972B (en) * | 2021-02-23 | 2023-03-14 | 农业农村部环境保护科研监测所 | Pulse plasma composite multistage water film deodorization device and deodorization method for breeding house |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: FUJIAN LAND OF ECOLOGICAL TECHNOLOGY INDUSTRIAL C Free format text: FORMER OWNER: DING RONGWU Effective date: 20080411 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20080411 Address after: Fengze District of Quanzhou city of Fujian province Dongtu Street Xinhua garden building C room 1201, zip code: 362000 Patentee after: Fujian Earth Ecological Technology Industry Co., Ltd. Address before: Licheng District of Quanzhou City, Fujian Province, Xiang Gong Xiang Zhuang CuO Cheng C No. 20, zip code: 362000 Patentee before: Ding Rongwu |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20040107 Termination date: 20100301 |