CN102423619A - Composite seawater desulfurization apparatus - Google Patents
Composite seawater desulfurization apparatus Download PDFInfo
- Publication number
- CN102423619A CN102423619A CN2011103127301A CN201110312730A CN102423619A CN 102423619 A CN102423619 A CN 102423619A CN 2011103127301 A CN2011103127301 A CN 2011103127301A CN 201110312730 A CN201110312730 A CN 201110312730A CN 102423619 A CN102423619 A CN 102423619A
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- Prior art keywords
- seawater
- desulfurization
- flue gas
- absorption tower
- area
- 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.)
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- 239000013535 sea water Substances 0.000 title claims abstract description 64
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 56
- 230000023556 desulfurization Effects 0.000 title claims abstract description 51
- 239000002131 composite material Substances 0.000 title abstract description 8
- 238000010521 absorption reaction Methods 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 238000000889 atomisation Methods 0.000 claims abstract description 18
- 150000001875 compounds Chemical class 0.000 claims description 11
- 238000012856 packing Methods 0.000 claims description 10
- 230000001788 irregular Effects 0.000 claims description 4
- 239000004033 plastic Substances 0.000 claims description 4
- 229920003023 plastic Polymers 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 239000000779 smoke Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000009825 accumulation Methods 0.000 claims description 3
- 239000003546 flue gas Substances 0.000 abstract description 33
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 32
- 239000000945 filler Substances 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 abstract 1
- 239000003595 mist Substances 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 10
- 230000008569 process Effects 0.000 description 6
- 230000003009 desulfurizing effect Effects 0.000 description 4
- 238000011161 development Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000035800 maturation Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008521 reorganization Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The present invention discloses a composite seawater desulfurization apparatus. According to the apparatus, a primary atomization and desulfurization area, a support frame, a secondary liquid film desulfurization area, a seawater distributer and a demisting area are sequentially arranged inside an absorption tower from bottom to top; the top of the absorption tower is provided with a flue gas outlet; the bottom of the absorption tower is provided with a flue gas inlet; the primary atomization and desulfurization area and the seawater distributer are connected with a seawater conveying system; in the secondary liquid film desulfurization area, on one hand, a filler surface provides a gas-liquid contact reaction surface to carry out seawater liquid film desulfurization, on the other hand, the flue gas is demisted, wherein the flue gas is subjected to a desulfurization treatment; the seawater distributer is characterized by: distributing the seawater to the filler in the fluid film desulfurization layer, and carrying out direct spraying desulfurization for the flue gas; the demisting area is provided with a demisting device to remove the mist droplets from the flue gas, and prevent the follow-up device from scaling. With the composite seawater desulfurization method and the apparatus thereof, the requirements of efficient desulfurization can be met, the use amount of the seawater and the filler can be saved, and the desulfurization cost can be reduced.
Description
Technical field
The present invention relates to flue gas desulfur device, relate in particular to a kind of seawater compound desulfurizer.
Background technology
SO
2Pollution is the subject matter of China's air environmental pollution, is the important environmental factor of the economic stable coordination development of restriction China.The source of SO2 in China's atmosphere mainly is a coal burning.Its discharge capacity accounts for more than 90% of total release, thereby the application of desulfur technology is very important for preserving the ecological environment, realize sustainable development.In present desulfur technology; Limestone-gypsum wet process of FGD technology has obtained using widely with characteristics such as its technology maturation, desulfuration efficiency are high, stable, but its system complex, floor space is big, the equipment corrosion blockage problem is relatively more serious, investment and operating cost height.
Maturation, raw material are easy to get, technology is simple, take up an area of less, reliable, advantages such as operating cost is lower, non-secondary pollution and the sea water desulfuration technology possesses skills.The seashore line length of China, coastal area economy are flourishing, and environmental protection requirement is strict.Engineerings such as coastal newly-built, reorganization and expansion power plant, steel plant are more, so the sea water desulfuration technology has wide practical use.
Traditional seawater desulfurizing process can be divided into flue gas system, the row's of confession sea water service system, SO
2Absorption system, seawater quality recovery system, measurement and control system.SO wherein
2The capital equipment of absorption system is the absorption tower, and packed bed is equipped with in inside, and the seawater that is sprayed into by tower top passes through packed bed and fully contacted by the flue gas that gets into (flowing) at the bottom of the tower from bottom to top, is convenient to SO
2Abundant absorption.Demister is equipped with in the absorption tower outlet, removes the molecules such as droplet in the flue gas, can reduce fouling and obstruction in GGH and back equipment.
Although traditional seawater desulfurizing process at home and abroad is applied,, except this technology only was fit to the abundant zone of seawater resources, its desulfuration efficiency was low, the seawater consumption is big, and filler need regularly clean and add.At present, mostly the filler that uses in China's seawater desulfurizing and absorption tower is external import, costs an arm and a leg, and system operation cost is high.Therefore, development of new sea water desulfuration technology is very necessary.
Summary of the invention
For overcoming the shortcoming and defect of prior art, the present invention provides a kind of simple in structure, rationally distributed seawater compound desulfurizer.
The present invention realizes through following technical proposals:
A kind of seawater compound desulfurizer; Comprise the absorption tower; Its characteristics are to be disposed with in the absorption tower primary atomization desulfurization zone, bracing frame, secondary liquid film desulfurization zone, seawater distributor from bottom to top, remove the fog-zone; The top on said absorption tower is provided with exhanst gas outlet, and bottom, said absorption tower is provided with smoke inlet, and said primary atomization desulfurization zone, seawater distributor are connected with salt water system.
Said primary atomization desulfurization zone is made up of the atomizer of a plurality of array distribution.
Said secondary liquid film desulfurization zone is made up of the packing layer that is deposited on the bracing frame.Said packing layer is that the unordered accumulation of the irregular collapsible or spiral PVC plastics of multilayer constitutes.
The said fog-zone of removing is made up of demister.The structure of said seawater distributor is identical with the structure of primary atomization desulfurization zone.
Compared with prior art, the invention has the beneficial effects as follows:
(1) primary atomization desulfurization zone and secondary liquid film desulfurization zone are realized the seawater composite desulfate, more effectively remove the SO in the flue gas
2, the consumption of saving seawater and filler, water-saving and electricity-saving reduces desulphurization cost.
(2) the primary atomization desulfurization zone is made up of atomizer efficiently, and seawater is atomized into fine particle, makes fully to mix with flue gas, reacts more abundant, effectively utilizes the space, absorption tower.
(3) secondary liquid film desulfurization zone provides reaction surface by filler on the one hand, makes the abundant haptoreaction of flue gas and seawater, and for for the flue gas behind the once desulfurization, packing layer also possesses except that fog effect on the other hand.
(4) owing to adopt the seawater composite desulfate, make the use amount of seawater and filler reduce, can reduce the thickness of secondary liquid film desulfurization zone, and then reduce the height on absorption tower.
(5) seawater distributor provides seawater to secondary liquid film desulfurization zone on the one hand, can also spray desulfurization to flue gas once more on the other hand.
(6) demister is further removed the molecules such as droplet in the flue gas, reduces fouling and obstruction in the equipment of GGH and back, has reduced maintenance cost.
This patent adopts simple and easy to do technological means, has good effect.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
Following specific embodiments of the invention is done further detailed explanation, but embodiment of the present invention is not limited thereto.
As shown in Figure 1.Seawater compound desulfurizer of the present invention; Be to be disposed with in the absorption tower primary atomization desulfurization zone 2, bracing frame 3, secondary liquid film desulfurization zone 4, seawater distributor 5 from bottom to top, remove fog-zone 6; The top on said absorption tower is provided with exhanst gas outlet 7; Bottom, said absorption tower is provided with smoke inlet 1, and said primary atomization desulfurization zone 2, seawater distributor 5 are connected with salt water system.
Said primary atomization desulfurization zone 2 is made up of the atomizer of a plurality of array distribution, and said secondary liquid film desulfurization zone 4 is made up of the packing layer that is deposited on the bracing frame 3.Said packing layer is that the unordered accumulation of the irregular collapsible or spiral PVC plastics of multilayer constitutes; Primary atomization desulfurization zone and secondary liquid film desulfurization zone are realized the seawater composite desulfate, more effectively remove the SO in the flue gas
2, the consumption of saving seawater and filler reduces desulphurization cost.
Removing fog-zone 6 is made up of demister.Increase except that further removing the molecules such as droplet in the flue gas in fog-zone 6, reduce fouling and obstruction in the equipment of GGH and back, reduced maintenance cost.
Said seawater distributor 5 provides seawater to secondary liquid film desulfurization zone on the one hand, can also spray desulfurization to flue gas once more on the other hand.
The primary atomization desulfurization zone is made up of atomizer efficiently, and seawater is atomized into fine particle, makes fully to mix with flue gas, reacts more abundant, effectively utilizes the space, absorption tower; Secondary liquid film desulfurization zone provides reaction surface by filler on the one hand, makes the abundant haptoreaction of flue gas and seawater, and for for the flue gas behind the once desulfurization, packing layer also possesses except that fog effect on the other hand.
Flue gas by inside, smoke inlet 1 entering absorption tower after, earlier, seawater is provided by salt water system 8 through primary atomization desulfurization zone 2, the atomizer array of primary atomization desulfurization zone 2 fully mixes with the seawater atomizing and with flue gas, and then removes the SO in the flue gas
2Flue gas through once desulfurization continues upwards to flow; Get into secondary liquid film desulfurization zone 4; Through the irregular collapsible or spiral PVC plastics of piling up the contact surface of reaction is provided, makes flue gas and seawater react fully, and then remove the SO in the flue gas once more
2, simultaneously, secondary liquid film desulfurization zone 4 can also carry out demist to the flue gas through once desulfurization.Make flue gas accomplish the seawater composite desulfate.
Flue gas is through after the above-mentioned seawater composite desulfate process, and flue gas is upwards through seawater distributor 5 and except that after 6 further processing of fog-zone, via exhanst gas outlet 7 discharge absorption towers.Afterwards, the seawater after the completion flue gas desulfurization converges to the bottom, absorption tower, and row promptly accomplishes the SO of seawater desulfurizing process to seawater quality recovery system 9
2Absorption process.
Just can realize this patent preferably as stated.
The foregoing description is a preferred implementation of the present invention; But embodiment of the present invention is not restricted to the described embodiments; Other any do not deviate from change, the modification done under spirit of the present invention and the principle, substitutes, combination, simplify; All should be the substitute mode of equivalence, be included within protection scope of the present invention.
Claims (6)
1. seawater compound desulfurizer; Comprise the absorption tower; It is characterized in that being disposed with in the absorption tower primary atomization desulfurization zone, bracing frame, secondary liquid film desulfurization zone, seawater distributor from bottom to top, remove the fog-zone; The top on said absorption tower is provided with exhanst gas outlet, and bottom, said absorption tower is provided with smoke inlet, and said primary atomization desulfurization zone, seawater distributor are connected with salt water system.
2. seawater compound desulfurizer according to claim 1 is characterized in that said primary atomization desulfurization zone is made up of the atomizer of a plurality of array distribution.
3. seawater compound desulfurizer according to claim 2 is characterized in that said secondary liquid film desulfurization zone is made up of the packing layer that is deposited on the bracing frame.
4. seawater compound desulfurizer according to claim 3 is characterized in that said packing layer is that the unordered accumulation of the irregular collapsible or spiral PVC plastics of multilayer constitutes.
5. seawater compound desulfurizer according to claim 4 is characterized in that the said fog-zone of removing is made up of demister.
6. seawater compound desulfurizer according to claim 5 is characterized in that said seawater dispenser arrangement in the packing layer top, is evenly distributed on the packing layer seawater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110312730.1A CN102423619B (en) | 2011-10-14 | 2011-10-14 | Composite seawater desulfurization apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110312730.1A CN102423619B (en) | 2011-10-14 | 2011-10-14 | Composite seawater desulfurization apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102423619A true CN102423619A (en) | 2012-04-25 |
| CN102423619B CN102423619B (en) | 2014-06-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110312730.1A Expired - Fee Related CN102423619B (en) | 2011-10-14 | 2011-10-14 | Composite seawater desulfurization apparatus |
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| Country | Link |
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| CN (1) | CN102423619B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104587914A (en) * | 2013-10-31 | 2015-05-06 | 中国中化股份有限公司 | Continuous atomization-gas-liquid and liquid film-gas-liquid reactor |
| CN107596870A (en) * | 2017-10-30 | 2018-01-19 | 东方电气集团东方锅炉股份有限公司 | A kind of flue gas desulfurization with seawater absorption tower |
| CN108837638A (en) * | 2018-06-21 | 2018-11-20 | 北京众鑫兴业大气污染治理有限公司 | Waste gas purification apparatus |
| CN109985477A (en) * | 2019-03-14 | 2019-07-09 | 赵德华 | Exhaust gas spray cleaning processing unit |
| CN112933881A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | High-specific-surface-area ship flue gas seawater desulfurization process and system |
| 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 |
| CN112933883A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | Ship flue gas photoelectrocatalysis seawater desulfurization process and system |
| CN112933884A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | High-specific-surface-area and photocatalytic marine flue gas seawater desulfurization process and system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1899675A (en) * | 2006-07-12 | 2007-01-24 | 陈玉乐 | Reverse flow type seawater desulfurizing and absorption tower |
| CN101822937A (en) * | 2010-05-11 | 2010-09-08 | 武汉科技学院 | Method for synchronous desulfurization and denitrification of marine vessel exhaust |
| CN201596455U (en) * | 2009-12-30 | 2010-10-06 | 国电科学技术研究院 | Movable-type seawater-desulfurization flue gas absorption device for industrial tests |
| CN202237776U (en) * | 2011-10-14 | 2012-05-30 | 华南理工大学 | Compound desulfurizing device by seawater |
-
2011
- 2011-10-14 CN CN201110312730.1A patent/CN102423619B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1899675A (en) * | 2006-07-12 | 2007-01-24 | 陈玉乐 | Reverse flow type seawater desulfurizing and absorption tower |
| CN201596455U (en) * | 2009-12-30 | 2010-10-06 | 国电科学技术研究院 | Movable-type seawater-desulfurization flue gas absorption device for industrial tests |
| CN101822937A (en) * | 2010-05-11 | 2010-09-08 | 武汉科技学院 | Method for synchronous desulfurization and denitrification of marine vessel exhaust |
| CN202237776U (en) * | 2011-10-14 | 2012-05-30 | 华南理工大学 | Compound desulfurizing device by seawater |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104587914A (en) * | 2013-10-31 | 2015-05-06 | 中国中化股份有限公司 | Continuous atomization-gas-liquid and liquid film-gas-liquid reactor |
| CN104587914B (en) * | 2013-10-31 | 2016-08-17 | 中国中化股份有限公司 | A kind of continuous way atomization gas-liquid, liquid film gas-liquid reactor |
| CN107596870A (en) * | 2017-10-30 | 2018-01-19 | 东方电气集团东方锅炉股份有限公司 | A kind of flue gas desulfurization with seawater absorption tower |
| CN108837638A (en) * | 2018-06-21 | 2018-11-20 | 北京众鑫兴业大气污染治理有限公司 | Waste gas purification apparatus |
| CN109985477A (en) * | 2019-03-14 | 2019-07-09 | 赵德华 | Exhaust gas spray cleaning processing unit |
| CN112933881A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | High-specific-surface-area ship flue gas seawater desulfurization process and system |
| 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 |
| CN112933883A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | Ship flue gas photoelectrocatalysis seawater desulfurization process and system |
| CN112933884A (en) * | 2021-03-02 | 2021-06-11 | 威海普益船舶环保科技有限公司 | High-specific-surface-area and photocatalytic marine flue gas seawater desulfurization process and system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102423619B (en) | 2014-06-11 |
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Granted publication date: 20140611 |