CN101757846B - Ship tail gas treatment method and device - Google Patents
Ship tail gas treatment method and device Download PDFInfo
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- CN101757846B CN101757846B CN2010101105002A CN201010110500A CN101757846B CN 101757846 B CN101757846 B CN 101757846B CN 2010101105002 A CN2010101105002 A CN 2010101105002A CN 201010110500 A CN201010110500 A CN 201010110500A CN 101757846 B CN101757846 B CN 101757846B
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- 238000000034 method Methods 0.000 title claims abstract description 47
- 239000007788 liquid Substances 0.000 claims abstract description 87
- 239000007789 gas Substances 0.000 claims abstract description 61
- 238000006243 chemical reaction Methods 0.000 claims abstract description 57
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000002912 waste gas Substances 0.000 claims abstract description 24
- 238000010992 reflux Methods 0.000 claims abstract description 23
- 238000009833 condensation Methods 0.000 claims abstract description 18
- 230000005494 condensation Effects 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 238000000889 atomisation Methods 0.000 claims abstract description 4
- 239000007787 solid Substances 0.000 claims description 45
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 30
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 20
- 238000006555 catalytic reaction Methods 0.000 claims description 18
- 239000000443 aerosol Substances 0.000 claims description 15
- 239000013618 particulate matter Substances 0.000 claims description 14
- 238000003672 processing method Methods 0.000 claims description 11
- 239000001569 carbon dioxide Substances 0.000 claims description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 10
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 8
- 238000011109 contamination Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 239000013535 sea water Substances 0.000 claims description 7
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 6
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 4
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 229910052787 antimony Inorganic materials 0.000 claims description 4
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 4
- 229910052741 iridium Inorganic materials 0.000 claims description 4
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052763 palladium Inorganic materials 0.000 claims description 4
- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 229910052703 rhodium Inorganic materials 0.000 claims description 4
- 239000010948 rhodium Substances 0.000 claims description 4
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 4
- 229910052707 ruthenium Inorganic materials 0.000 claims description 4
- 229910052718 tin Inorganic materials 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 238000000975 co-precipitation Methods 0.000 claims description 3
- 229910017052 cobalt Inorganic materials 0.000 claims description 3
- 239000010941 cobalt Substances 0.000 claims description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 3
- 238000000703 high-speed centrifugation Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 8
- 239000000428 dust Substances 0.000 description 7
- 239000003344 environmental pollutant Substances 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 5
- 150000001450 anions Chemical class 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- 241001074085 Scophthalmus aquosus Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000003113 dilution method Methods 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 238000005184 irreversible process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
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- 230000000630 rising effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The invention relates to the technical field of environmental protection, in particular to a novel ship tail gas treatment device; it comprises the following steps: the device comprises a water pump, an electro-catalytic treatment unit, a storage tank, an atomization device, a gas-liquid reaction device, a solid-liquid separation device, a condensation reflux device, a waste gas inlet and a pump; the water outlet of the water pump is connected with the electro-catalytic treatment unit, the electro-catalytic treatment unit is connected with the storage tank, one end of the pump is connected with the storage tank, the other end of the pump is connected with the atomizing device, the atomizing device is connected with the liquid input end of the gas-liquid reaction device, the waste gas inlet is connected with the gas input end of the gas-liquid reaction device, the gas output end of the gas-liquid reaction device is connected with the condensation reflux device, the upper end of the condensation reflux device is provided with an exhaust port, the liquid output end of the gas-liquid reaction device is connected with the input end of the solid-liquid. The invention also discloses a tail gas treatment method, which has the following advantages: the energy consumption is low, the efficiency is high, the installation is convenient, and the operation is simple; the reaction product has no pollution and better removal effect.
Description
Technical field
The present invention relates to environmental technology field, especially a kind of novel ship exhaust gas treating method and device.
Background technology
Atmospheric environment is the valuable resource that the mankind depend on for existence, and the destruction of atmospheric environment resource is a kind of irreversible process, recovers good atmosphere quality than the Air Pollution of taking measures fundamentally and pays more economic cost.Yet in the modern society, the damage ratio of atmosphere is more serious, traces it to its cause, and atmosphere pollution mainly contains several kinds of dust granules, carbon dioxide, sulfur dioxide or nitrogen oxide etc.
Boats and ships operation meeting needs a large amount of fuel, can produce a large amount of accessory substances during fuel combustion, like dust, carbon dioxide (CO
2), nitrogen oxide (NO
x) and sulfur dioxide (SO
2) wait pernicious gas.These noxious gas emissions can seriously influence human beings'health in atmosphere, also can hinder the growth of plant, thereby cause the severe contamination of earth environment.
Carbon dioxide is greenhouse gases, and scientist's prediction is because greenhouse effects; To the year two thousand fifty global temperatures with rising 2-4 degree centigrade, iceberg, polar region, north and south will be melted significantly, cause the sea level to be risen greatly; Some island countries and coastal cities will be flooded in water; Comprising several famous international big cities: New York, Shanghai, Tokyo and Sydney.
SO
2And NO
xBe the main atmosphere pollution that forms acid rain and acid mist, ecological environment and health are had significant damage.
Just because of as above reason, people have just had the technology of various control atmosphere pollution.
The technology of administering pollutant is to the difference of pollutant and difference.
The main method that particulate pollutant is administered is: to the particulate pollutant size, mainly contain 4 types of dry method, wet method, filtration and static, the most frequently used is exactly sack cleaner (filtration), cyclone dust collector (dry method), bubble dust collector (wet method) etc.Along with the raising that efficiency of dust collection is required, electrostatic precipitation is also progressively brought into use.
Owing to had a large amount of nitrogen oxide, oxysulfide in the atmosphere, atmosphere pollution just taken place, so produced contamination accident a piece by a piece.Scientist is to the character of this type oxide, and the technology that has proposed contaminated solution has absorption process, absorption method, condensation method, catforming, firing method, biological clarification, membrane separation process and dilution method.
Yet, regrettably, in the prior art, have all basically that equipment cost has high input, pollutant removing efficient is low, can not remove carbon nitrogen amounts of sulphur contaminants or the like shortcoming simultaneously.
Summary of the invention
For addressing the above problem, the object of the present invention is to provide a kind of ship tail gas processing method, and disclose a kind of ship tail gas treating apparatus by this, it can remove the polluter in the ship tail gas effectively.
Method of the present invention and device adopt following technical scheme to realize:
A kind of ship tail gas processing method is characterized in that comprising following process:
The process of A, generation rinse water: fresh seawater is handled, produced rinse water efficiently;
B, atomization process: the rinse water entering atomising device that the A process is made atomizes, and obtains aerosol;
C, gas-liquid reaction process: the aerosol that the B process is obtained sends into gas-liquid reaction apparatus and ship tail gas reacts, thereby removes the gaseous contamination material in the waste gas; When aerosol forms liquid when solid particulate matter in the waste gas contacts on solid particulate matter, and then coprecipitation is gone into the bottom of reaction unit;
D, Separation of Solid and Liquid process: the solidliquid mixture that bottom in the C process is obtained separates, and obtains solid particle and liquid.
Above-mentioned described ship tail gas processing method, its characteristic are that also gaseous contamination material described in the process C is one or more the mixture in carbon dioxide, nitrogen oxide, the oxysulfide.
Above-mentioned described ship tail gas processing method, its characteristic be that also the ship tail gas described in the process C is getting into before the gas-liquid reaction apparatus, is the process that removes of carrying out solid particle.Like this, solid removal efficient is higher.
A kind of novel ship exhaust gas processing device is characterized in that it comprises: suction pump 1, electro-catalysis processing unit 2, storage tank 3, atomising device 4, gas-liquid reaction apparatus 5, equipment for separating liquid from solid 6, condensation reflux unit 7, exhaust gas entrance 8 and pump 10; The delivery port of suction pump 1 links to each other with the import of electro-catalysis processing unit 2; The outlet of electro-catalysis processing unit 2 is connected with storage tank 3 through pipeline, and pump 10 1 ends are connected with storage tank 3, and the other end links to each other with the import of atomising device 4; The outlet of atomising device 4 connects the liquid input of gas-liquid reaction apparatus 5; Exhaust gas entrance 8 connects the gas input of gas-liquid reaction apparatus 5, and the gas output end of gas-liquid reaction apparatus 5 connects condensation reflux unit 7, and condensation reflux unit 7 upper ends have exhaust outlet 11; The liquid output of gas-liquid reaction apparatus 5 connects the input of equipment for separating liquid from solid 6, offers solid discharge mouth 13 and liquid discharge outlet 12 on the equipment for separating liquid from solid 6.
Above-mentioned described ship tail gas treating apparatus, the atomizing type that it is characterized in that said atomising device 7 are ultrasonic atomizatio or high speed centrifugation atomizing.
Above-mentioned described ship tail gas treating apparatus is characterized in that the surface of described electro-catalysis processing unit 2 scribbles rare metal.
Above-mentioned described ship tail gas treating apparatus is characterized in that described rare metal is one or more in iridium, platinum, titanium, palladium, rhodium, ruthenium, tin, antimony, cobalt or the lead.
Above-mentioned described ship tail gas treating apparatus is characterized in that described gas-liquid reaction apparatus 5 is a kind of one or more levels reaction units.
Above-mentioned described ship tail gas treating apparatus is characterized in that described gas-liquid reaction apparatus 5 top design have condensation reflux unit.
The operation principle of this device is: suction pump 1 is transported to electro-catalysis processing unit 2 to seawater through pipeline; Seawater reacts in electro-catalysis processing unit 2 the insides, produces active rinse water, and active rinse water gets into storage tank 3; Start pump 10; Be transported to atomising device 4 to active rinse water, produce aerosol, be transported to gas-liquid reaction apparatus 5 enclosure interior.
Exhaust pipe is transported to waste gas the gas-liquid reaction apparatus 5 from exhaust gas entrance 8, meets with the active rinse water aerosol that gushes out in the air-flow uphill process, reacts, and removes the polluter in the waste gas.
Because the temperature of waste gas is very high, so, have the part rinse water and be evaporated to steam, rise with air-flow, so also have in the water-soluble steam of part polluter.Air-flow arrives in the condensation reflux unit 7 at last, condensing reflux, and the polluter of dissolving refluxes, and improves removal efficiency.The gas of cleaning is discharged from exhaust outlet 11.
Reaction rinse water is later discharged from gas-liquid reaction apparatus 5 bottoms, gets into equipment for separating liquid from solid 6, and solid particulate matter and fluid separation applications wherein, solid particulate matter is discharged from solid discharge mouth 13, and liquid is discharged from liquid discharge outlet 12.
In gas-liquid reaction apparatus 5 the insides, can clean the solid particulate matters such as dust in the waste gas simultaneously and remove.
The rinse water that flows out from gas-liquid reaction apparatus 5 bottoms is guided to equipment for separating liquid from solid 6 by the road, removes the turbid materials such as solid particulate matter in the rinse water; The solid particulate matter individual processing of separating.
In the gas-liquid reaction apparatus 5, aerosol is fully contacted with ascending air, remove the polluter in the waste gas to greatest extent; Handle tail gas after up to standard through discharge of pipes.
Atomising device 7 first-selected ultrasonic atomizatio modes in apparatus of the present invention, its atomizing effect is good, and grain diameter is littler, and can produce a large amount of anions simultaneously.Anion is electrically charged, and better active suction-operated is arranged, and is better to the cleaning performance that pollutes waste gas, and cleaning efficiency is high.
Do not add any chemical substance among the present invention; Raw material sources are simple; Energy consumption is low, and efficient is high; Easy for installation, simple to operate; Product is pollution-free, and the oxysulfide removal efficiency reaches more than 90%, and the removal of nitrogen oxide rate reaches more than 80%, and the carbon dioxide eliminating rate reaches more than 70%; Removal effect is very good.
Description of drawings
Fig. 1 is the structural representation of apparatus of the present invention embodiment.
The specific embodiment
Embodiment one is the embodiment of the inventive method; Embodiment two is the embodiment of apparatus of the present invention.
Embodiment one
A kind of ship tail gas processing method is characterized in that comprising following process:
The process of A, generation rinse water: fresh seawater is handled, produced rinse water efficiently;
B, atomization process: the rinse water entering atomising device that the A process is made atomizes, and obtains aerosol;
C, gas-liquid reaction process: the aerosol that the B process is obtained sends into gas-liquid reaction apparatus and ship tail gas reacts, thereby removes the gaseous contamination material in the waste gas; When aerosol forms liquid when solid particulate matter in the waste gas contacts on solid particulate matter, and then coprecipitation is gone into the bottom of reaction unit;
D, Separation of Solid and Liquid process: the solidliquid mixture that bottom in the C process is obtained separates, and obtains solid particle and liquid.
Above-mentioned described ship tail gas processing method, its characteristic are that also gaseous contamination material described in the process C is one or more the mixture in carbon dioxide, nitrogen oxide, the oxysulfide.
Above-mentioned described ship tail gas processing method, its characteristic be that also the ship tail gas described in the process C is getting into before the gas-liquid reaction apparatus, is the process that removes of carrying out solid particle.Like this, solid removal efficient is higher.
Embodiment two
See also Fig. 1 and reference implementation instance one; A kind of novel ship exhaust gas processing device is characterized in that it comprises: suction pump 1, electro-catalysis processing unit 2, storage tank 3, atomising device 4, gas-liquid reaction apparatus 5, equipment for separating liquid from solid 6, condensation reflux unit 7, exhaust gas entrance 8 and pump 10; The delivery port of suction pump 1 links to each other with the import of electro-catalysis processing unit 2; The outlet of electro-catalysis processing unit 2 is connected with storage tank 3 through pipeline, and pump 10 1 ends are connected with storage tank 3, and the other end links to each other with the import of atomising device 4; The outlet of atomising device 4 connects the liquid input of gas-liquid reaction apparatus 5; Exhaust gas entrance 8 connects the gas input of gas-liquid reaction apparatus 5, and the gas output end of gas-liquid reaction apparatus 5 connects condensation reflux unit 7, and condensation reflux unit 7 upper ends have exhaust outlet 11; The liquid output of gas-liquid reaction apparatus 5 connects the input of equipment for separating liquid from solid 6, offers solid discharge mouth 13 and liquid discharge outlet 12 on the equipment for separating liquid from solid 6.
Above-mentioned described ship tail gas treating apparatus, the atomizing type that it is characterized in that said atomising device 7 are ultrasonic atomizatio or high speed centrifugation atomizing.
Above-mentioned described ship tail gas treating apparatus is characterized in that the surface of described electro-catalysis processing unit 2 scribbles rare metal.
Above-mentioned described ship tail gas treating apparatus is characterized in that described rare metal is at least a in iridium, platinum, titanium, palladium, rhodium, ruthenium, tin, antimony, brill or the lead.
Above-mentioned described ship tail gas treating apparatus is characterized in that described gas-liquid reaction apparatus 5 is a kind of one or more levels reaction units.
Above-mentioned described ship tail gas treating apparatus is characterized in that described gas-liquid reaction apparatus 5 top design have condensation reflux unit.
The operation principle of apparatus of the present invention is: suction pump 1 is transported to electro-catalysis processing unit 2 to seawater through pipeline; Seawater reacts in electro-catalysis processing unit 2 the insides, produces active rinse water, and active rinse water gets into storage tank 3; Start pump 10; Be transported to atomising device 4 to active rinse water, produce aerosol, be transported to gas-liquid reaction apparatus 5 enclosure interior.
Exhaust pipe is transported to waste gas the gas-liquid reaction apparatus 5 from exhaust gas entrance 8, meets with the active rinse water aerosol that gushes out in the air-flow uphill process, reacts, and removes the polluter in the waste gas.
Because the temperature of waste gas is very high, so, have the part rinse water and be evaporated to steam, rise with air-flow, so also have in the water-soluble steam of part polluter.Air-flow arrives in the condensation reflux unit 7 at last, condensing reflux, and the polluter of dissolving refluxes, and improves removal efficiency.The gas of cleaning is discharged from exhaust outlet 11.
Reaction rinse water is later discharged from gas-liquid reaction apparatus 5 bottoms, gets into equipment for separating liquid from solid 6, and solid particulate matter and fluid separation applications wherein, solid particulate matter is discharged from solid discharge mouth 13, and liquid is discharged from liquid discharge outlet 12.
In gas-liquid reaction apparatus 5 the insides, can clean the solid particulate matters such as dust in the waste gas simultaneously and remove.
The rinse water that flows out from gas-liquid reaction apparatus 5 bottoms is guided to equipment for separating liquid from solid 6 by the road, removes the turbid materials such as solid particulate matter in the rinse water; The solid particulate matter individual processing of separating.
In the gas-liquid reaction apparatus 5, aerosol is fully contacted with ascending air, remove the polluter in the waste gas to greatest extent; Handle tail gas after up to standard through discharge of pipes.
In gas-liquid reaction apparatus 5 the insides, the carbon dioxide (CO in rinse water and the waste gas
2), nitrogen oxide (NO
x), oxysulfide (SO
x) wait abundant contact, react, product is soluble in water, to the reaction unit bottom, gets into next process with washing water flow then.
High-temp waste gas is met water can produce a large amount of steam; Steam rises with the steam of handling; Like this, what remaining polluter can continue in the waste gas combines with drops of water vapor, so the condensing reflux system that is provided with among the present invention; Make steam carry pollutant condensing reflux together, improved the waste gas absorption efficiency.
Atomising device 7 first-selected ultrasonic atomizatio modes in apparatus of the present invention, its atomizing effect is good, and grain diameter is littler, and can produce a large amount of anions simultaneously.Anion is electrically charged, and better active suction-operated is arranged, and is better to the cleaning performance that pollutes waste gas, and cleaning efficiency is high.
Do not add any chemical substance among the present invention; Raw material sources are simple; Energy consumption is low, and efficient is high; Easy for installation, simple to operate; Product is pollution-free, and the oxysulfide removal efficiency reaches more than 90%, and the removal of nitrogen oxide rate reaches more than 80%, and the carbon dioxide eliminating rate reaches more than 70%; Removal effect is very good.
Concrete effect sees the following form:
| Pollutant | Content before cleaning | Clean back content | Cleaning efficiency |
| Sulfur dioxide (PPM) | 723.6 | 48.5 | 93.3％ |
| Nitrogen oxide (PPM) | 167.7 | 26.9 | 84.0％ |
| Carbon dioxide (%) | 5.47 | 1.36 | 75.1％ |
Clear specifically exemplary embodiment of the present invention of this paper and present preferred implementation should be appreciated that design of the present invention can be by other various forms enforcement utilizations, and they drop in protection scope of the present invention equally.
Claims (9)
1. ship tail gas processing method is characterized in that comprising following process:
A, produce the process of rinse water: fresh seawater is fed in the electro-catalysis processing unit react; Produce rinse water, wherein the surface of electro-catalysis processing unit scribbles one or more in rare metal iridium, platinum, titanium, palladium, rhodium, ruthenium, tin, antimony, cobalt or the lead;
B, atomization process: the rinse water entering atomising device that the A process is made atomizes, and obtains aerosol;
C, gas-liquid reaction process: the aerosol that the B process is obtained sends into gas-liquid reaction apparatus and ship tail gas reacts, thereby removes the gaseous contamination material in the waste gas; When aerosol forms liquid when solid particulate matter in the waste gas contacts on solid particulate matter, and then coprecipitation is gone into the bottom of reaction unit;
D, Separation of Solid and Liquid process: the solidliquid mixture that obtains of bottom in the C process is separated, obtain solid particle and liquid is discharged.
2. ship tail gas processing method according to claim 1 is characterized in that gaseous contamination material described in the process C is one or more the mixture in carbon dioxide, nitrogen oxide, the oxysulfide.
3. ship tail gas processing method according to claim 1 is characterized in that the ship tail gas described in the process C exists
Before the entering gas-liquid reaction apparatus, be the process that removes of carrying out solid particle.
4. a ship tail gas treating apparatus is characterized in that it comprises: suction pump (1), electro-catalysis processing unit (2), storage tank (3), atomising device (4), gas-liquid reaction apparatus (5), equipment for separating liquid from solid (6), condensation reflux unit (7), exhaust gas entrance (8) and pump (10); The delivery port of suction pump (1) links to each other with the import of electro-catalysis processing unit (2); The outlet of electro-catalysis processing unit (2) is connected with storage tank (3) through pipeline; Pump (10) one ends are connected with storage tank (3); The other end links to each other with the import of atomising device (4), and the outlet of atomising device (4) connects the liquid input of gas-liquid reaction apparatus (5), and exhaust gas entrance (8) connects the gas input of gas-liquid reaction apparatus (5); The gas output end of gas-liquid reaction apparatus (5) connects condensation reflux unit (7); Condensation reflux unit (7) upper end has exhaust outlet (11), and the liquid output of gas-liquid reaction apparatus (5) connects the input of equipment for separating liquid from solid (6), offers solid discharge mouth (13) and liquid discharge outlet (12) on the equipment for separating liquid from solid (6).
5. ship tail gas treating apparatus according to claim 4, the atomizing type that it is characterized in that said atomising device (7) are ultrasonic atomizatio or high speed centrifugation atomizing.
6. ship tail gas treating apparatus according to claim 4 is characterized in that the surface of described electro-catalysis processing unit (2) scribbles rare metal.
7. ship tail gas treating apparatus according to claim 6 is characterized in that described rare metal is at least a in iridium, platinum, titanium, palladium, rhodium, ruthenium, tin, antimony, cobalt or the lead.
8. ship tail gas treating apparatus according to claim 4 is characterized in that described gas-liquid reaction apparatus (5) is a kind of one or more levels reaction unit.
9. ship tail gas treating apparatus according to claim 4 is characterized in that condensation reflux unit is arranged at described gas-liquid reaction apparatus (5) top.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101105002A CN101757846B (en) | 2010-02-10 | 2010-02-10 | Ship tail gas treatment method and device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101105002A CN101757846B (en) | 2010-02-10 | 2010-02-10 | Ship tail gas treatment method and device |
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| CN101757846B true CN101757846B (en) | 2012-04-11 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI123737B (en) | 2012-02-13 | 2013-10-15 | Oy Langh Ship Ab | Method for treating ship-source contaminants with a scrubber |
| CN103657301B (en) * | 2013-12-27 | 2016-06-08 | 云立方秦皇岛科技有限公司 | A kind of uncontrollable discharge ultra-fine grain dust foam suppressing dust with dry mist technique |
| US9387438B2 (en) | 2014-02-14 | 2016-07-12 | Tenneco Automotive Operating Company Inc. | Modular system for reduction of sulphur oxides in exhaust |
| CN104043327B (en) * | 2014-06-21 | 2016-08-24 | 曹学良 | A kind of ship tail gas electro-catalysis processing system |
| CN106139863A (en) * | 2016-08-11 | 2016-11-23 | 大连海事大学 | A kind of marine exhaust integrated treatment recovery system |
| CN106315500A (en) * | 2016-09-28 | 2017-01-11 | 青岛丽星物流有限公司 | Device and method for cleaning wharf air |
| CN112933882A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | Marine flue gas electro-catalysis seawater desulfurization process and system |
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| CN101091873A (en) * | 2007-04-21 | 2007-12-26 | 大连理工大学 | Technical method by using seawater to remove sulfur dioxide in smoke through membrane absorption method |
| CN101104130A (en) * | 2007-08-01 | 2008-01-16 | 大连海事大学 | Device and method for treating ship tail gas with sea water washing |
| CN101314106A (en) * | 2008-06-13 | 2008-12-03 | 彭斯干 | Method and apparatus for desulfurizing exhaust gas of seagoing vessel |
| CN201744291U (en) * | 2010-02-10 | 2011-02-16 | 青岛海德威科技有限公司 | Novel ship tail gas treatment device |
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