CN2207872Y - pneumatic emulsification filter - Google Patents
pneumatic emulsification filter Download PDFInfo
- Publication number
- CN2207872Y CN2207872Y CN 94221426 CN94221426U CN2207872Y CN 2207872 Y CN2207872 Y CN 2207872Y CN 94221426 CN94221426 CN 94221426 CN 94221426 U CN94221426 U CN 94221426U CN 2207872 Y CN2207872 Y CN 2207872Y
- Authority
- CN
- China
- Prior art keywords
- platen
- air inlet
- liquid
- cyclone
- pneumatic emulsifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000004945 emulsification Methods 0.000 title abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 238000009826 distribution Methods 0.000 claims abstract description 10
- 230000001804 emulsifying effect Effects 0.000 claims description 28
- 239000004744 fabric Substances 0.000 claims description 10
- 239000000839 emulsion Substances 0.000 claims description 9
- 230000006698 induction Effects 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 17
- 239000000428 dust Substances 0.000 abstract description 14
- 230000003009 desulfurizing effect Effects 0.000 abstract description 5
- 238000009792 diffusion process Methods 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 22
- 239000002912 waste gas Substances 0.000 description 9
- 230000000505 pernicious effect Effects 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000010438 granite Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 235000012538 ammonium bicarbonate Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- KIZFHUJKFSNWKO-UHFFFAOYSA-M calcium monohydroxide Chemical compound [Ca]O KIZFHUJKFSNWKO-UHFFFAOYSA-M 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 235000020985 whole grains Nutrition 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
A pneumatic emulsification filter comprises an exhaust hood 1, a liquid distribution pipe 2, an upper platen 3, a pneumatic emulsification filter element 4, a lower platen 5, an air inlet diffusion section 6, an air inlet and liquid outlet elbow 7 and the like, wherein two ends of the pneumatic emulsification filter element 4 are respectively arranged on mounting holes of the upper platen and the lower platen, the upper platen and the lower platen are arranged at 120 degrees by three screws, the upper platen and the lower platen are fastened, the exhaust hood 1 is connected with the upper platen 3, the small end of the air inlet diffusion section 6 is connected with the air inlet and liquid outlet elbow 7, the large end of the air inlet diffusion section is connected with the lower platen 5, and the liquid distributor 2 is arranged in the exhaust. The filter has dust removing rate up to 99% and desulfurizing rate up to 75-90%. Small volume, long service life, water and energy saving.
Description
The Pneumatic emulsifying filter belongs to liquid and separates the particle of disperse and the chemical purifying device of smog, flue gas or exhaust as release agent from gas, air or steam.
Exhaust gas discharged such as existing coal-burning boiler, metallurgical furnace, ceramic kiln, cement kiln contain pernicious gases such as a large amount of dust and SO2, NOx, CO2, and they are the primary pollution source of atmospheric environment, also are the main sources that produces acid rain.China and countries in the world all take much count of the improvement of these pollution sources.The device of Chalk-dust filtering and purifying harmful gas mainly contains gallet water curtain dust collector and spraying type dust-removing desulfurating apparatus etc. simultaneously.Though they have certain dust-removal and desulfurizing ability, but its weak point is: no matter waste gas is by moisture film, spraying area or by water-bath, the stroke of waste gas contact water (liquid) is very short, reach certain dedusting, the purpose of purifying harmful gas, must strengthen the attaching space of waste gas and liquid or the combination of employing multiple technologies, make structure of filter complexity or system huge like this, water consumption also increases.As China patent No. ZL92219420.3(CN2127637Y) " granite water dust scrubber ", it is become by the granite shaped material combinatorial surface, comprise turnover tracheae, annular water tank and dash cover, water inlet pipe, shower, scaffold etc., dust removal efficiency can reach more than 98%, and the ability of removing and harmful gas is arranged.Its weak point is that this device volume is bigger, and water consumption is also big.China's patent 91229244.X(CN2114502U and for example) " ma stone rotary deduster ", it is that moisture film, steam spray, water sprays, the dust arrester of water-bath combination, this device dust removal efficiency reaches 99.9%, but it is bigger that its weak point is a volume, water consumption is also big, also need the steam supply, promoting conforms is restricted.China's patent 89106517.2(CN1049616A for another example) " method and apparatus of industry smoke comprehensive purifying and dedusting ", it is the device of spray, water-bath combination, dust-removal and desulfurizing denitrogenation etc. is designed to one, but its volume is still bigger, also need outer power drive rotary fan to separate air water (dirt), and dedusting, desulfurization degree are not very good, and operating cost is higher relatively.
The purpose of this utility model is a kind of filter of Pneumatic emulsifying efficiently that has the while dust-removal and desulfurizing and purify other pernicious gas of design.
The purpose of this utility model is achieved in that the Pneumatic emulsifying filter is made up of hood, liquid distribution pipe, upper platen, Pneumatic emulsifying filter element, lower platen, air inlet diffuser and air inlet discharge opeing elbow etc.It will be loaded with the waste gas of dust and pernicious gas (SO2, NOx etc.) by the specific swirl-flow devices of a cover, produce the high speed swirling eddy, to pulverize by the dirty unstable liquid in filter top, form gas-liquid two-phase turbulent flow (real process is a gas, liquid, solid body particle three-phase stream), with water film dedusting, the several times of spraying and dedusting gas-liquid mixed formation, tens of times mixing stroke, gas-liquid is fully mixed, reach the emulsification degree, thereby improved the ability of liquid trap exhaust gas and dust and pernicious gas greatly.
The utility model has the advantages that:
1. dust-removal and desulfurizing rate height, dedusting are suitable for the wholegrain footpath, and dust removal efficiency reaches more than 99%, and desulfurization degree reaches 75-95%; 2. can be applicable to dried, humid gas and high temperature, the easy various media of dewfall; 3. dedusting, desulfurization constitute one, and filter volume is little, long service life (element uses more than 5 years); 4. water consumption is few, captures dust, and the water of pernicious gas (or other liquid 70-80%) can be recycled, and whole system is saved water and energy; 5. working service is convenient, and is cheap.
Accompanying drawing of the present utility model has:
Fig. 1 Pneumatic emulsifying filter structure schematic representation.
Fig. 2 Pneumatic emulsifying filter A-A generalized section.
Fig. 3 Pneumatic emulsifying filter element structural representation.
Fig. 4 hydrocyclone structure schematic diagram.
Fig. 5 liquid distribution pipe structural representation.
Below in conjunction with drawings and Examples the utility model is further described:
Referring to Fig. 1 and Fig. 2, this Pneumatic emulsifying filter is made up of hood 1, liquid distribution pipe 2, upper platen 3, Pneumatic emulsifying filter element 4, lower platen 5, air inlet diffuser 6 and air inlet discharge opeing elbow 7 etc.The two ends of Pneumatic emulsifying filter element 4 are contained in respectively on the installing hole of upper platen 3 and lower platen 5, and become 120 ° of distributions with three screw rods, upper platen 3 and lower platen 5 are fastened, hood 1 usefulness flange is connected with upper platen 3, be contained in the top of upper platen 3, it is the gathering and the discharge-channel of the gas after Pneumatic emulsifying filter element 4 filters, the small end of air inlet diffuser 6 is connected with air inlet discharge opeing elbow 7 with flange, big end is connected with lower platen 5 with flange, and air inlet diffuser 6 and air inlet discharge opeing elbow 7 are inlet channels of processed waste gas.It simultaneously is again the discharge-channel that purifies emulsion.The Pneumatic emulsifying filter is the size according to the filtering gas volume flow, is made up of several or tens of Pneumatic emulsifying filter elements 4.For the convenience of installing, generally constitute one group (as shown in Figure 2), and adopt modular system with seven, with adapt to handle the flow that varies in size (as from 1 ton to hundreds of tons steam boiler exhaust gas discharged amount) needs.Liquid distribution pipe 2 is suitable with the structure of Pneumatic emulsifying filter element 4, so that liquid is imported.Liquid distribution pipe 2 is contained in the hood 1.
Referring to Fig. 3, Fig. 4 and Fig. 5, Pneumatic emulsifying filter element 4 is made up of air induction conduit 8, cyclone 9, emulsion band pipe 10, cloth liquid platen 11 and air guide catheter 12 etc., and it is the critical component of Pneumatic emulsifying filter.Air induction conduit 8 is contained in the below of cyclone 9, and it is one
100 to
200 straight-through pipe is the passage that waste gas enters Pneumatic emulsifying filter element 4.Cyclone 9 joins with an end of emulsion band pipe 10, the other end of emulsion band pipe 10 and cloth liquid platen 11 join, cloth liquid platen 11 joins with air guide catheter 12, and cyclone 9 is by 3-50 blade 13 (blade 13 is 20～70 ° with the angle α of cyclone shell 14 walls) and cyclone shell 14(internal diameter at a certain angle
100-
200) constitute one.It is the element that produces the high speed swirling eddy.Cloth liquid platen 11 is Circular Plate that a through hole accounts for 50 ° 70% of whole platen area, is beneficial to form cascade.Emulsion band pipe 10 with air guide catheter 12 is and the straight pipe of cyclone 9 with the footpath.Emulsion band pipe 10 provides the pipeline of emulsion process.Air guide catheter 12 is that the liquid of liquid distribution pipe 2 dispensings is supplied with the passage of cloth liquid platen 11 by even tube wall, is again the passing away through emulsion band pipe 10 purified gases.
The course of work of Pneumatic emulsifying filter is as follows:
Waste gas enters air inlet diffuser 6 by air inlet discharge opeing elbow 7, and after diffusion, after making waste gas enter Pneumatic emulsifying filter element 4 uniformly to filter, Purge gas is discharged by hood 1.This Pneumatic emulsifying filter adopts new Pneumatic emulsifying principle, the waste gas that is loaded with dust and pernicious gas (as SO2, NOx etc.) produces the high speed swirling eddy by cyclone 9 in Pneumatic emulsifying filter element 4, cloth liquid platen 11 dirty unstable liquids are pulverized, formation gas-liquid two-phase turbulent flow, gas-liquid is fully mixed, reach the degree of emulsification, thereby improved the ability of liquid trap exhaust gas and dust greatly, its capture rate can reach more than 99%; In like manner, the efficient of its absorption pernicious gas also improves greatly, adopts different absorption liquids, can make the efficient of filtering noxious gas reach 75-95% or more than.Filter absorption (absorption) liquid, the general water that adopts cheapness, the difference according to filtering (collection) pernicious gas can add inorganic acid, alkali, inorganic salts or simple organic solvent in water.As remove SO2, during available CaCO3 micro mist, CaOH, NH4HCO3 or other aqueous slkali are done and absorbent.Desulfurization degree can reach 75-95% or more than, in and the absorbent consumption calculate by the chemical balance formula of removing the SO2 amount, add about 10% again.
Claims (2)
1, a kind of Pneumatic emulsifying filter, it is characterized in that: by hood (1), liquid distribution pipe (2), upper platen (3), Pneumatic emulsifying filter element (4), lower platen (5), air inlet diffuser (6) and air inlet discharge opeing elbow (7) are formed, the two ends of Pneumatic emulsifying filter element (4) are contained in respectively on the installing hole of upper platen (3) and lower platen (5), and become 120 ° of configurations with three screw rods, upper platen (3) and lower platen (5) are fastened, hood (1) is connected with upper platen (3) with flange, be contained in upper platen (3) top, the small end of air inlet diffuser (6) is connected with flange with air inlet discharge opeing elbow (7), big end is connected with flange with lower platen (5), and liquid distribution pipe (2) is contained in the hood (1).
2, Pneumatic emulsifying filter according to claim 1, it is characterized in that: above-mentioned Pneumatic emulsifying filter element (4) is by air induction conduit (8), cyclone (9) with 3-50 blade (13), emulsion band pipe (10), cloth liquid platen (11), air guide catheter (12) is formed, air induction conduit (8) is contained in the below of cyclone (9), one end of emulsion band pipe (10) and cyclone (9) join, the other end and cloth liquid platen (11) join, cloth liquid platen (11) joins with air guide catheter (12), the through hole of annular cloth liquid platen (11) accounts for 50～70% of whole platen area, the angle α of the wall of cyclone (9) shell (14) and blade (13) is 20 °-70 °, and blade (13) constitutes one with cyclone (9) shell (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94221426 CN2207872Y (en) | 1994-09-19 | 1994-09-19 | pneumatic emulsification filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94221426 CN2207872Y (en) | 1994-09-19 | 1994-09-19 | pneumatic emulsification filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2207872Y true CN2207872Y (en) | 1995-09-20 |
Family
ID=33835728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 94221426 Expired - Fee Related CN2207872Y (en) | 1994-09-19 | 1994-09-19 | pneumatic emulsification filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2207872Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101406805B (en) * | 2007-10-12 | 2011-09-14 | 中国航天空气动力技术研究院 | Pneumatic desulfuration unit |
| CN101406801B (en) * | 2007-10-12 | 2012-11-21 | 中国航天空气动力技术研究院 | Parallel combination structure of pneumatic desulfuration unit |
| CN113546496A (en) * | 2021-07-15 | 2021-10-26 | 株洲舒创环保技术有限公司 | Ultra-clean filter for smoke particulate matter |
-
1994
- 1994-09-19 CN CN 94221426 patent/CN2207872Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101406805B (en) * | 2007-10-12 | 2011-09-14 | 中国航天空气动力技术研究院 | Pneumatic desulfuration unit |
| CN101406801B (en) * | 2007-10-12 | 2012-11-21 | 中国航天空气动力技术研究院 | Parallel combination structure of pneumatic desulfuration unit |
| CN113546496A (en) * | 2021-07-15 | 2021-10-26 | 株洲舒创环保技术有限公司 | Ultra-clean filter for smoke particulate matter |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |