CN102407075A - Waste gas treating device - Google Patents
Waste gas treating device Download PDFInfo
- Publication number
- CN102407075A CN102407075A CN2011104398601A CN201110439860A CN102407075A CN 102407075 A CN102407075 A CN 102407075A CN 2011104398601 A CN2011104398601 A CN 2011104398601A CN 201110439860 A CN201110439860 A CN 201110439860A CN 102407075 A CN102407075 A CN 102407075A
- Authority
- CN
- China
- Prior art keywords
- water
- gas
- storage tank
- aqueous vapor
- pipe
- 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.)
- Granted
Links
- 239000002912 waste gas Substances 0.000 title claims abstract description 32
- 238000003860 storage Methods 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000007789 gas Substances 0.000 claims abstract description 34
- 239000002253 acid Substances 0.000 claims abstract description 21
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 239000002351 wastewater Substances 0.000 claims abstract description 8
- 238000000926 separation method Methods 0.000 claims description 12
- 239000003595 mist Substances 0.000 claims description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 238000005070 sampling Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 5
- 239000004033 plastic Substances 0.000 claims description 5
- 229920003023 plastic Polymers 0.000 claims description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 2
- 239000011152 fibreglass Substances 0.000 claims description 2
- -1 polyethylene Polymers 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 1
- 239000007864 aqueous solution Substances 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 150000003254 radicals Chemical class 0.000 abstract 1
- 239000007921 spray Substances 0.000 description 8
- 235000011114 ammonium hydroxide Nutrition 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
The invention relates to a waste gas treating device which comprises a waste gas collecting pipe 6, wherein the waste gas collecting pipe 6 is used for collecting waste gas into a water-gas exchange pipe 2 under the action of a Roots blower 1; a plurality of water-gas exchange holes 3 are uniformly distributed at the lower surface, close to the bottom of a water storage tank 7, of the water-gas exchange pipe 2; the water-gas exchange pipe 2 is submerged in the middle of the water in the water storage tank 7; water is injected from a water inlet pipe 9 to the water storage tank 7 till reaching an upper-limit water level; and a water outlet pipe 10 is used for exchanging waste water. The waste gas treating device is characterized in that a water-gas separating leakage control plate 4a is arranged at a position about 8-10 centimeters higher than the liquid level of the water storage tank 7; a plurality of gas-leaking holes 8a are uniformly distributed on the water-gas separating leakage control plate 4a; the diameters of the gas-leaking holes 8a are 6-8 millimeters; and cleaned gas is discharged from an exhaust pipe 5 through the gas-leaking holes 8a. The water-gas separating leakage-control plate and the water-gas exchange holes are arranged, thereby efficiently preventing the water in the water storage tank from being in direct contact with air, simultaneously discharging the gas from the gas-leaking holes, greatly increasing the contact volume and time between the waste gas and water through the water-gas exchange pipe, and fully mixing the water with the gas in the water storage tank. The acid radicals, carbonic oxide and sulfur dioxide in the waste gas are fully absorbed by an aqueous solution in the water storage tank, the zero emission of the waste gas is substantially achieved, the service life of equipment is prolonged and the environment is optimized.
Description
Technical field
The present invention relates to a kind of treating apparatus of waste exhaust gases.
Background technology
At present, in electroplating electrolysis and diamond purge process, the use of acid is essential; So, will form very big acid mist acid gas at workshop so, if untimely processing; Human body there is injury, environment is also damaged, also easy simultaneously etching apparatus.At present; For the employing of acids treatment of waste gas great majority is the mode of spray; Shower water through circulation constantly sprays, and can reduce acid ion to a certain extent toward airborne discharge capacity, but exist equally the acid mist gas that flies away is arranged in the air; And damage when part appears in spray head, will occur part dead angle spray less than situation.Can't reach completely and to handle, influence air quality, can't accomplish the production of environmental protection, cleaning, employee's health is also had injury in various degree.Simultaneously, this waste gas has bigger corrosion to production equipment, and the equipment availability is extremely low, influences the service life of equipment.
At utility model patent Granted publication CN201168551Y, the aqueous vapor isolating construction of a kind of acid group emission-control equipment of patent name has adopted the spray mode that acid group gas is sprayed, and utilizes metal woven screen that aqueous vapor is filtered.This mode has improvement slightly than the mode of traditional spray; But still there is the spray dead angle; During spray the time of contact of waste gas and water short, the defective that acid ion can't merge with water fully, simultaneously; Metal woven screen receives the corrosion influence of acid group, cause can't be lasting, handle acid mist comprehensively, completely.
Summary of the invention
[0004] the present invention is intended to reduce the halfway problem of prior art exhaust-gas treatment, reduces airborne acid mist content greatly.The technical scheme that the present invention takes is: a kind of emission-control equipment; Comprise that gas sampling pipe 6 is through roots blower 1 collection waste gas to aqueous vapor exchange pipe 2; Aqueous vapor exchange pipe 2 is submerged in the water liquid middle part of aqua storage tank 7, gets into aqua storage tank 7 from water inlet pipe 9 water fillings, and outlet pipe 10 is used to change waste water; The 8-10 centimeters is provided with aqueous vapor separation control bushing 4a on aqua storage tank 7 liquid levels; On aqueous vapor separation control bushing 4a, be uniformly distributed with several leakage holes 8a, leakage hole 8a aperture is the 6-8 millimeter, sees through leakage hole 8a and discharges clean airs from blast pipe 5.This aqueous vapor is separated the setting of control bushing; Make equipment in running status; Water in the aqua storage tank 7 receives under the gas pressure powerful in the aqueous vapor exchange pipe 2, exchanges the bottom that the gas of managing in 2 is pressed into aqua storage tank 7 by aqueous vapor, when gas upwards moves, runs into the resistance that aqueous vapor is separated the control bushing again; Gas and water are mixed once more, make in the waste gas with acid group, carbon monoxide, sulfur dioxide be adsorbed in the water fully.Like this, both stopped effectively that water directly contacted with air in the aqua storage tank, and can let gas from leakage hole, discharge again simultaneously, improved greatly, and made water and gas fused fully in aqua storage tank from the contact volume of waste gas through aqueous vapor exchange Guan Yushui.
Top 7-9 centimetre of said aqueous vapor separation control bushing 4a is provided with second aqueous vapor separation control bushing 4b, controls bushing 4b second aqueous vapor separation and is uniformly distributed with several leakage holes two 8b, and the aperture of leakage hole two 8b is the 8-10 millimeter.Second aqueous vapor separated the control bushing, on first basis, strengthened the effect that aqueous vapor is separated more; The fused time of waste gas and water is longer; Acid group, carbon monoxide, sulfur dioxide are adsorbed in the water liquid, fused more abundant, reach better exhaust-gas treatment effect.
The following bottom direction of aqua storage tank 7 of leaning on of said aqueous vapor exchange pipe 2 is uniformly distributed with several aqueous vapor exchange holes 3.Aqueous vapor exchange hole 3 is the contacts area that increased waste gas and water, the contacting with water of stereoscopic and omnibearing.Said aqueous vapor exchange pipe 2 is made as the 10-15 root; These aqueous vapor exchange pipes 2 add several aqueous vapor exchange holes 3; Increase thousands of times contact area than traditional shower, added that roots blower increases the effect of blast, in aqua storage tank, formed some gas columns; Make the fusion of water and waste gas more thorough, more comprehensive.
The waste gas that described gas sampling pipe 6 is collected is acid mist, carbon monoxide, sulfur dioxide, but is not limited to.
Described aqua storage tank 7 is an anticorrosive, for a kind of in plastics, fiberglass, polyethylene, the stainless steel but be not limited to.
Described aqua storage tank 7 is for square, circular or taper but be not limited to;
Said waste gas is acid mist, and the material of aqua storage tank 7 is plastics, in aqua storage tank 7 water, adds alkali, and pH value is 10-14.
Description of drawings
Accompanying drawing 1 emission-control equipment sketch map
Accompanying drawing 2 aqueous vapors exchange pipe and aqueous vapor exchange hole A-A profile
1 roots blower, 2 aqueous vapors exchange pipe, 3 aqueous vapor exchange hole 4a aqueous vapors are separated second aqueous vapor of control bushing 4b and are separated control bushing 5 blast pipes 6 gas sampling pipes 7 aqua storage tank 8a leakage hole 8b leakage holes 29 water inlet pipes 10 outlet pipes.
The specific embodiment
Like Fig. 1, shown in Figure 2
Embodiment 1, a kind of emission-control equipment; Handle the acid group class waste gas after electroplating, aqua storage tank 7 adopts the cylindrical can of plastic material, gets into aqua storage tank 7 from water inlet pipe 9 water fillings; The height of water filling is the last waterline of aqua storage tank height; Separate control bushing 4a with aqueous vapor and be separated by 20 centimetres, in water, add sheet alkali simultaneously, transferring pH value is 12; Collect acid group class waste gas by gas sampling pipe 6, collect waste gas to aqueous vapor exchange pipe 2 through roots blower 1 supercharging, aqueous vapor exchange pipe 2 is 10, and all is submerged in the water liquid middle part of aqua storage tank 7; Below aqueous vapor exchange pipe, lean on the bottom direction of aqua storage tank 7 to be uniformly distributed with several aqueous vapor exchange holes 3; 10 centimeters are provided with an aqueous vapor separation control bushing 4a on aqua storage tank 7 waters surface; On aqueous vapor separation control bushing 4a, be uniformly distributed with several leakage holes 8a; Leakage hole 8a aperture is 8 millimeters, sees through leakage hole 8a and discharges clean air from blast pipe 5, and outlet pipe 10 is used to change waste water.
2 one kinds of emission-control equipments of embodiment; Handle the waste gas of the carbon monoxide class of thermal power plant generation; Aqua storage tank 7 adopts the cylindrical can of stainless steel materials, and all contact with ammoniacal liquor and all adopt stainless steel material, corrodes preventing; Annotate ammoniacal liquor from water inlet pipe 9 and get into aqua storage tank 7, the height of ammoniacal liquor is 2/3rds of an aqua storage tank height; Collect carbon monoxide class waste gas by gas sampling pipe 6, collect waste gas to aqueous vapor exchange pipe 2 through roots blower 1, aqueous vapor exchange pipe 2 is 12, and all is submerged in the water liquid middle part of aqua storage tank 7; Below aqueous vapor exchange pipe, lean on the bottom direction of aqua storage tank 7 to be uniformly distributed with several aqueous vapor exchange holes 3; 10 centimeters are provided with an aqueous vapor separation control bushing 4a on aqua storage tank 7 waters surface; On aqueous vapor separation control bushing 4a, be uniformly distributed with several leakage holes 8a; Leakage hole 8a aperture is 8 millimeters, and 7 centimeters are provided with second same aqueous vapor separation control bushing 4b on first simultaneously, are uniformly distributed with several leakage holes two 8b above; The waste gas of carbon monoxide class and ammoniacal liquor fully merge in aqua storage tank 7, see through leakage hole 8a and discharge clean air from blast pipe 5.
This aqueous vapor is separated the setting of control bushing and aqueous vapor exchange hole; Both stopped effectively that water directly contacted with air in the aqua storage tank; Simultaneously can let gas from leakage hole, discharge again; Improved greatly from the contact volume of waste gas, made water and gas fused fully in aqua storage tank through aqueous vapor exchange Guan Yushui.Like this, treatment of waste gas reaches zero-emission basically, and equipment operating efficiency is high, and long service life has been optimized environment.
Claims (8)
1. emission-control equipment; Comprise that gas sampling pipe (6) is through roots blower (1) collection waste gas to aqueous vapor exchange pipe (2); Aqueous vapor exchange pipe (2) is submerged in the water liquid middle part of aqua storage tank (7), gets into aqua storage tank (7) from water inlet pipe (9) water filling, and outlet pipe (10) is used to change waste water; It is characterized in that: aqua storage tank (7) above the liquid level 8-10 centimeters aqueous vapor be set separate control bushing (4a); On aqueous vapor separation control bushing (4a), be uniformly distributed with several leakage holes (8a), the aperture of leakage hole (8a) is the 6-8 millimeter, sees through leakage hole (8a) and discharges clean air from blast pipe (5).
2. emission-control equipment according to claim 1; It is characterized in that: top 7-9 centimetre of said aqueous vapor separation control bushing (4a) is provided with second aqueous vapor and separates control bushing (4b); Separate control bushing (4b) second aqueous vapor and be uniformly distributed with several leakage holes two (8b), the aperture of leakage hole two (8b) is the 8-10 millimeter.
3. emission-control equipment according to claim 1 is characterized in that: the following bottom direction of aqua storage tank (7) of leaning on of said aqueous vapor exchange pipe (2) is uniformly distributed with several aqueous vapor exchange holes (3).
4. emission-control equipment according to claim 1 is characterized in that: said aqueous vapor exchange pipe (2) is made as the 10-15 root.
5. emission-control equipment according to claim 1 is characterized in that: the waste gas that described gas sampling pipe (6) is collected is acid mist, carbon monoxide, sulfur dioxide, but is not limited to.
6. emission-control equipment according to claim 1 is characterized in that: described aqua storage tank (7) is an anticorrosive, for a kind of in plastics, fiberglass, polyethylene, the stainless steel but be not limited to.
7. emission-control equipment according to claim 1 is characterized in that: described aqua storage tank (7) is for square, circular or taper but be not limited to.
8. emission-control equipment according to claim 1 is characterized in that: said waste gas is acid mist, and the material of aqua storage tank (7) is plastics, adds sheet alkali in aqua storage tank (7) the water liquid, and the accent pH value is 10-14.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110439860 CN102407075B (en) | 2011-12-26 | 2011-12-26 | Waste gas treating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110439860 CN102407075B (en) | 2011-12-26 | 2011-12-26 | Waste gas treating device |
Publications (2)
Publication Number | Publication Date |
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CN102407075A true CN102407075A (en) | 2012-04-11 |
CN102407075B CN102407075B (en) | 2013-07-10 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201110439860 Expired - Fee Related CN102407075B (en) | 2011-12-26 | 2011-12-26 | Waste gas treating device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102929164A (en) * | 2012-10-26 | 2013-02-13 | 中联重科股份有限公司 | Control method, device and system for waste gas collection |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040208802A1 (en) * | 2003-04-16 | 2004-10-21 | Shuichi Kanno | Catalytic exhaust gas decomposition apparatus and exhaust gas decomposition method |
CN201036628Y (en) * | 2007-05-30 | 2008-03-19 | 北京三辰环卫机械有限公司 | Deodorizing device for vacuum dung-suction vehicle |
CN201091817Y (en) * | 2007-07-30 | 2008-07-30 | 黄高英 | Off-gases disposal device |
CN201168551Y (en) * | 2008-03-28 | 2008-12-24 | 上海宝钢天通磁业有限公司 | Water-gas separation structure of acid radical waste gas treater |
CN202438254U (en) * | 2011-12-26 | 2012-09-19 | 长沙石立超硬材料有限公司 | Waste gas treatment device |
-
2011
- 2011-12-26 CN CN 201110439860 patent/CN102407075B/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040208802A1 (en) * | 2003-04-16 | 2004-10-21 | Shuichi Kanno | Catalytic exhaust gas decomposition apparatus and exhaust gas decomposition method |
CN201036628Y (en) * | 2007-05-30 | 2008-03-19 | 北京三辰环卫机械有限公司 | Deodorizing device for vacuum dung-suction vehicle |
CN201091817Y (en) * | 2007-07-30 | 2008-07-30 | 黄高英 | Off-gases disposal device |
CN201168551Y (en) * | 2008-03-28 | 2008-12-24 | 上海宝钢天通磁业有限公司 | Water-gas separation structure of acid radical waste gas treater |
CN202438254U (en) * | 2011-12-26 | 2012-09-19 | 长沙石立超硬材料有限公司 | Waste gas treatment device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102929164A (en) * | 2012-10-26 | 2013-02-13 | 中联重科股份有限公司 | Control method, device and system for waste gas collection |
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CN102407075B (en) | 2013-07-10 |
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Granted publication date: 20130710 |