CN103908865B - Waste gas trapping back-fire relief heat sink - Google Patents
Waste gas trapping back-fire relief heat sink Download PDFInfo
- Publication number
- CN103908865B CN103908865B CN201410152473.3A CN201410152473A CN103908865B CN 103908865 B CN103908865 B CN 103908865B CN 201410152473 A CN201410152473 A CN 201410152473A CN 103908865 B CN103908865 B CN 103908865B
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- China
- Prior art keywords
- high pressure
- gas
- positive blower
- pressure positive
- waste gas
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- 239000002912 waste gas Substances 0.000 title claims abstract description 28
- 239000007789 gas Substances 0.000 claims abstract description 29
- 239000003599 detergent Substances 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 4
- 229910052751 metal Inorganic materials 0.000 claims abstract description 4
- 239000002184 metal Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 11
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000003595 mist Substances 0.000 claims description 6
- 239000001569 carbon dioxide Substances 0.000 claims description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 4
- 239000000428 dust Substances 0.000 claims description 3
- 239000008187 granular material Substances 0.000 claims description 3
- 239000005431 greenhouse gas Substances 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000000779 smoke Substances 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 230000005540 biological transmission Effects 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 230000002000 scavenging effect Effects 0.000 claims description 2
- 230000000903 blocking effect Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Ventilation (AREA)
- Chimneys And Flues (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
Waste gas of the present invention trapping back-fire relief heat sink.At present when carrying out the trapping of heat treatment waste gas, there is the situation in high-temperature exhaust emission source, the temperature of emission source at this moment is the highest, there is disaster hidden-trouble.Including: casing (7), described box house is provided with metal gauze demister (3), there is bottom described box house alkaline detergent solution (1), air inlet (8) is had on described casing, gas outlet (9), high pressure positive blower (4) is installed on described casing, described high pressure positive blower side, bottom surface has through hole, described air inlet is connected with high pressure positive blower bottom surface port, described gas outlet is connected with outlet pipe (2), described high pressure positive blower side through hole is connected with admission line (6), described backblast pipe (5) is immersed in alkaline detergent solution.The present invention is used for cooling when waste gas traps and fire preventing.
Description
Technical field:
The present invention relates to a kind of waste gas trapping back-fire relief heat sink.
Background technology:
At present when carrying out the trapping of heat treatment waste gas, there is the situation in high-temperature exhaust emission source, the temperature of emission source at this moment is the highest, there is disaster hidden-trouble.Comprising a lot of sour gas and dust granules in waste gas, carbon dioxide is most commonly seen simultaneously, and carbon dioxide is the main cause causing greenhouse effect, and global warming will threaten the existence of the mankind, and it is necessary for therefore processing carbon dioxide in waste gas.
The way of traditional back-fire relief heat sink many employings Water spray, it is desirable to operating rate is low, device bulky, inefficiency;In terms of cooling and solution greenhouse gas emission, effect is undesirable;Gas attack after process is strong, and secondary pollution is serious.
Summary of the invention:
It is an object of the invention to provide a kind of waste gas trapping back-fire relief heat sink.
Above-mentioned purpose is realized by following technical scheme:
A kind of waste gas trapping back-fire relief heat sink, its composition includes: casing, described box house is provided with metal gauze demister, bottom described box house, there is alkaline detergent solution, air inlet, gas outlet is had on described casing, on described casing, high pressure positive blower is installed, described high pressure positive blower side, bottom surface have through hole, described air inlet is connected with high pressure positive blower bottom surface port, described gas outlet is connected with outlet pipe, described high pressure positive blower side through hole is connected with admission line, and described backblast pipe is immersed in alkaline detergent solution.
Waste gas trapping back-fire relief cool-down method, the Negotiation speed of waste gas is less than 3m/s, and waste gas sends into casing at air inlet through high pressure positive blower, and the pressure of high-pressure blast is 2000pa to 3000pa, and the flow of high pressure positive blower is 2000m3/h.Gas settles through air inlet pipeline, the area 0.4m of air inlet pipeline2Above, a length of more than 600mm, the degree of depth entering liquid is more than 50mm.Entering into alkaline detergent solution through air inlet pipeline effluent air, eliminate harmful gas therein, the composition of described alkaline detergent solution is based on sodium hydroxide, and the ph value of alkaline detergent solution is 7.5.Described gas carries out the process of water smoke through tinsel except mist net, and described tinsel is 50mm except the thickness of mist net, and installation interval is 50mm, most preferably 4 layers, and initial resistance is 50pa.
Waste gas trapping back-fire relief cool-down method, during work, waste gas enters the temperature of blower fan less than 80 degrees Celsius, the orifice diameter entering water diverter is 1mm, gas flow rate through demister is less than 3m/s, the blower fan of back-fire relief heat sink is equipped with and should ensure that work wind speed is less than 3m/s, solves resistance 2000pa, including the leading portion resistance of ducting.
Beneficial effect:
1. the present invention utilizes high pressure positive blower will thoroughly to block flame transmission in other introducing alkaline detergent solutions of thermal-flame, EGT is down to the temperature levels of cleaning mixture simultaneously, outlet temperature is less than 45 degrees Celsius, pro-alkaline oxide in scavenging and dust granules, through the process of multilamellar demister, the humidity of exit gas is less than 85%.
2. the present invention can quickly block flame propagation, good cooling effect, and Outlet Gas Temperature is close to wash temperature, and carbon dioxide absorption rate, more than 95%, reduces greenhouse gas emission effective, and discharging gas does not has secondary pollution.
Accompanying drawing 1 is the structural representation of the present invention.
Detailed description of the invention:
Embodiment 1:
A kind of waste gas trapping back-fire relief heat sink, its composition includes: casing 7, described box house is provided with metal gauze demister 3, there is bottom described box house alkaline detergent solution 1, air inlet 8 is had on described casing, gas outlet 9, high pressure positive blower 4 is installed on described casing, described high pressure positive blower side, bottom surface has through hole, described air inlet is connected with high pressure positive blower bottom surface port, described gas outlet is connected with outlet pipe 2, described high pressure positive blower side through hole is connected with admission line 6, described backblast pipe 5 is immersed in alkaline detergent solution.
Embodiment 2:
Trapping back-fire relief cool-down method according to the waste gas described in embodiment 1, the Negotiation speed of waste gas is less than 3m/s, and waste gas sends into casing at air inlet through high pressure positive blower, and the pressure of high-pressure blast is 2000pa to 3000pa, and the flow of high pressure positive blower is 2000m3/h.Gas settles through air inlet pipeline, the area 0.4m of air inlet pipeline2Above, a length of more than 600mm, the degree of depth entering liquid is more than 50mm.Entering into alkaline detergent solution through air inlet pipeline effluent air, eliminate harmful gas therein, the composition of described alkaline detergent solution is based on sodium hydroxide, and the ph value of alkaline detergent solution is 7.5.Described gas carries out the process of water smoke through tinsel except mist net, and described tinsel is 50mm except the thickness of mist net, and installation interval is 50mm, most preferably 4 layers, and initial resistance is 50pa.A kind of equipment utilizing claim 1 carries out waste gas trapping back-fire relief cool-down method, it is characterized in that: during work, waste gas enters the temperature of blower fan less than 80 degrees Celsius, the orifice diameter entering water diverter is 1mm, gas flow rate through demister is less than 3m/s, the blower fan of back-fire relief heat sink is equipped with and should ensure that work wind speed is less than 3m/s, solves resistance 2000pa, including the leading portion resistance of ducting.
Embodiment 3:
Back-fire relief cool-down method is trapped according to the waste gas described in embodiment 1 or 2, during work, waste gas enters the temperature of blower fan less than 80 degrees Celsius, the orifice diameter entering water diverter is 1mm, gas flow rate through demister is less than 3m/s, the blower fan of back-fire relief heat sink is equipped with and should ensure that work wind speed is less than 3m/s, solves resistance 2000pa, including the leading portion resistance of ducting.
Claims (1)
1. a waste gas trapping back-fire relief heat sink, its composition includes: casing, it is characterized in that: described box house is provided with metal gauze demister, bottom described box house, there is alkaline detergent solution, air inlet is had on described casing, gas outlet, on described casing, high pressure positive blower is installed, described high pressure positive blower side, bottom surface has through hole, described air inlet is connected with the through hole of high pressure positive blower bottom surface, described gas outlet is connected with outlet pipe, described high pressure positive blower side through hole is connected with admission line, the gas outlet of high pressure positive blower is connected with the air inlet of backblast pipe, described backblast pipe is immersed in alkaline detergent solution;
Utilize high pressure positive blower to be introduced by thermal-flame in alkaline detergent solution and thoroughly block flame transmission, EGT is down to the temperature levels of cleaning mixture simultaneously, outlet temperature is less than 45 degrees Celsius, pro-alkaline oxide in scavenging and dust granules, through the process of multilamellar demister, the humidity of exit gas is less than 85%;
The Negotiation speed of waste gas is less than 3m/s, and waste gas sends into casing at air inlet through high pressure positive blower, and the pressure of high-pressure blast is 2000pa to 3000pa, and the flow of high pressure positive blower is 2000m3/ h, gas settles through backblast pipe, the area 0.4m of backblast pipe2 Above, a length of more than 600mm, the degree of depth entering liquid is more than 50mm, enters into alkaline detergent solution through backblast pipe effluent air, harmful gas therein is eliminated, the composition of described alkaline detergent solution is based on sodium hydroxide, and the ph value of alkaline detergent solution is 7.5, and described gas carries out the process of water smoke through tinsel except mist net, described tinsel is 50mm except the thickness of mist net, installation interval is 50mm, most preferably 4 layers, and initial resistance is 50pa;
During work, waste gas enters the temperature of high pressure positive blower and is less than 80 degrees Celsius, and the gas flow rate through demister should ensure that work wind speed is less than 3m/s less than 3m/s, the high pressure positive blower outfit of back-fire relief heat sink, solves resistance 2000pa, including the leading portion resistance of ducting;
Quickly blocking flame to propagate, good cooling effect, Outlet Gas Temperature is close to wash temperature, and carbon dioxide absorption rate, more than 95%, reduces greenhouse gas emission effective, and discharging gas does not has secondary pollution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410152473.3A CN103908865B (en) | 2014-04-16 | 2014-04-16 | Waste gas trapping back-fire relief heat sink |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410152473.3A CN103908865B (en) | 2014-04-16 | 2014-04-16 | Waste gas trapping back-fire relief heat sink |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103908865A CN103908865A (en) | 2014-07-09 |
| CN103908865B true CN103908865B (en) | 2017-01-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410152473.3A Active CN103908865B (en) | 2014-04-16 | 2014-04-16 | Waste gas trapping back-fire relief heat sink |
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| Country | Link |
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| CN (1) | CN103908865B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61209024A (en) * | 1985-03-13 | 1986-09-17 | Mitsubishi Heavy Ind Ltd | Method for preventing white smoke of oil mist bleed fan |
| JPS6359336A (en) * | 1986-08-29 | 1988-03-15 | Kyowa Kako Kk | Treatment of silane type special material gas |
| JPH08318118A (en) * | 1995-05-25 | 1996-12-03 | Honda Motor Co Ltd | Flue gas dust collector for welding |
| CN2378104Y (en) * | 1999-06-11 | 2000-05-17 | 刘子川 | Wet-type smoke prevention desulfuration dust collector |
| CN2412159Y (en) * | 2000-03-17 | 2000-12-27 | 罗正凡 | Water-bath silk net efficiency dust catcher |
| CN2714134Y (en) * | 2003-09-23 | 2005-08-03 | 中国疾病预防控制中心环境与健康相关产品安全所 | Wet type dust remover |
| CN201744298U (en) * | 2010-08-10 | 2011-02-16 | 西安市窑炉设备研究所 | Integral smoke purifier for brickfield kilns |
| CN203220831U (en) * | 2013-05-14 | 2013-10-02 | 魏界民 | Liquid medium air purifying device for purifying PM (particulate matter) 2.5 |
-
2014
- 2014-04-16 CN CN201410152473.3A patent/CN103908865B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61209024A (en) * | 1985-03-13 | 1986-09-17 | Mitsubishi Heavy Ind Ltd | Method for preventing white smoke of oil mist bleed fan |
| JPS6359336A (en) * | 1986-08-29 | 1988-03-15 | Kyowa Kako Kk | Treatment of silane type special material gas |
| JPH08318118A (en) * | 1995-05-25 | 1996-12-03 | Honda Motor Co Ltd | Flue gas dust collector for welding |
| CN2378104Y (en) * | 1999-06-11 | 2000-05-17 | 刘子川 | Wet-type smoke prevention desulfuration dust collector |
| CN2412159Y (en) * | 2000-03-17 | 2000-12-27 | 罗正凡 | Water-bath silk net efficiency dust catcher |
| CN2714134Y (en) * | 2003-09-23 | 2005-08-03 | 中国疾病预防控制中心环境与健康相关产品安全所 | Wet type dust remover |
| CN201744298U (en) * | 2010-08-10 | 2011-02-16 | 西安市窑炉设备研究所 | Integral smoke purifier for brickfield kilns |
| CN203220831U (en) * | 2013-05-14 | 2013-10-02 | 魏界民 | Liquid medium air purifying device for purifying PM (particulate matter) 2.5 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103908865A (en) | 2014-07-09 |
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Inventor after: Ge Weihan Inventor before: Ge Weihan |
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