CN2346494Y - Smoke, SO2 absorbing appts, by seawater process - Google Patents
Smoke, SO2 absorbing appts, by seawater process Download PDFInfo
- Publication number
- CN2346494Y CN2346494Y CN 98235799 CN98235799U CN2346494Y CN 2346494 Y CN2346494 Y CN 2346494Y CN 98235799 CN98235799 CN 98235799 CN 98235799 U CN98235799 U CN 98235799U CN 2346494 Y CN2346494 Y CN 2346494Y
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- precooler
- absorber
- flue gas
- sulfur dioxide
- cooling medium
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Abstract
The utility model relates to a sulfur dioxide absorbing apparatus by a seawater process, comprising a smoke precooler and a sulfur dioxide absorber. A smoke channel is arranged between the precooler and the sulfur dioxide absorber, the precooler has a discharging channel for discharging coolant and the absorber has a discharging channel for discharging water. The utility model has the advantages of high absorption efficiency of sulfur dioxide and low cost of production and operation.
Description
The utility model relates to apparatus for absorbing SO 2 from fume by seawater method, belongs to environmental protection technical field, is applicable to the occasion of the acid pollution materials such as sulfur dioxide in the facility institute discharged flue gas such as eliminating coastal industry device such as thermal power plant coal-burning boiler.
Because the needs of environmental protection control acid rain must remove sulfur in smoke that industrial equipment discharges such as fire coal.Prior art is to install flue gas desulfurization equipment additional on above-mentioned industrial plants, and these flue gas desulfur devices all must use certain sulfur dioxide absorbent, with the absorbing and removing sulfur in smoke.Natural sea-water is because natural alkalinity that it had makes it become cheap and good sulfur dioxide absorbent, thus make coastal industrial plants use cheap and efficiently desulfuration of flue gas by sea water technology had advantageous supremacy clause.The desulfuration of flue gas by sea water device, with the natural sea-water flue gas that spray washing flows through in absorber that extracts, the clean flue gas that has been washed sulfur dioxide can directly enter atmosphere by chimney; Washed the draining behind the sulfur dioxide,, therefore its quality recovery can have been entered the nature marine site after satisfying environmental requirement because wherein the minute quantity sulfate that increases is safe and harmless for marine environment.Because the flue gas that is washed is to come from commercial plant such as coal-burning boiler, the cigarette temperature often surpasses 130 ℃ Celsius, can not directly absorb the operation of sulfur dioxide to it, so must carry out pre-cooled to flue gas.Existing seawater method apparatus for absorbing SO 2 (Fig. 6), because its precooler is positioned at below, absorber inside, because of having absorbed the pre-cooled water that flue gas heat has higher water temperature, converge at absorber bottom and the acid seawater that has absorbed sulfur dioxide, thereby offseted pre-cooled effect, the sulfur dioxide that causes dissolving in liquid phase is overflowed again, thereby causes system's desulfuration efficiency to descend.Simultaneously, because the spray facility of absorber is located at precooler top, thereby must corresponding lifting as the lift of the seawater of absorbent, the rising significantly that this has just caused systematic running cost to use.Because desulfuration efficiency is low and the high critical defect of operating cost, the use of said apparatus is subjected to strict restriction.
The purpose of this utility model is, overcomes the deficiencies in the prior art, improves the process structure of desulfuration of flue gas by sea water device, make its can be more efficiently, build at low cost and move.
The technical scheme of apparatus for absorbing SO 2 from fume by seawater method of the present utility model is: it comprises precooler and absorber, and precooler discharge cooling medium and absorber draining have passing away separately.It is achieved in that precooler and absorber constitute (Fig. 2) by two cavitys respectively, between two cavitys exhaust gases passes is arranged, and precooler discharge cooling medium and absorber draining are provided with passing away separately.Precooler and absorber also can be two independent tower bodies (Fig. 3), have exhaust gases passes to connect between two tower bodies, and precooler discharge cooling medium and absorber draining are provided with passing away separately.The cooling medium that precooler uses can be that water for industrial use, seawater, air or other are suitable for use as the liquid or the gas of cooling medium.The heat absorption mode of precooler can be cooling medium directly spray (Fig. 2, Fig. 3) or with cooling medium by heat exchange element absorb heat (Fig. 4, Fig. 5).Precooler can be that flue gas enters pipe self formation.When the heat absorption mode of precooler was the structure of absorbing heat by heat exchange element with cooling medium, precooler can be located at the absorber below and be arranged at same tower body (Fig. 5) with absorber, and cooling medium also can have independent passing away.
Accompanying drawing of the present utility model and being described as follows:
Fig. 1, be the schematic diagram that the utility model device connects with other parts;
Fig. 2, constitute by two cavitys and schematic diagram when using the fountain precooler for the utility model;
Fig. 3, constitute by two independent tower bodies and schematic diagram when using the fountain precooler for the utility model;
Fig. 4, constitute by two independent tower bodies and schematic diagram when using heat exchange element formula precooler for the utility model;
Fig. 5, constitute by same tower body and schematic diagram when using heat exchange element formula precooler for the utility model;
Fig. 6, be existing seawater method apparatus for absorbing SO 2.
Among the figure: 1, burner such as boiler, 2, electric precipitator, 3, air-introduced machine, 4, flue gas enters pipe, and 5, precooler, 6, exhaust gases passes, 7, absorber, 8, smoke outlet tube, 9, chimney, 10, cooling medium enters pipe, and 11, shower or heat exchange element, 12, hot cooling medium passing away, 13, sea water pump, 14, absorber advances the seawater pipe, and 15, the absorber drainage channel, 16, the quality recovery device.
Operation principle of the present utility model is: the flue gas that burners such as boiler (1) are discharged is removed wherein dust through electric precipitator (2) earlier, after air-introduced machine (3) supercharging, enter pipe (4) input precooler (5) again, enter absorber (7) via exhaust gases passes (6) with the SO in the washing flue gas through the flue gas of supercooling from flue gas
2, the clean flue gas after the washing is discharged into chimney (9) from absorber (7) top through smoke outlet tube (8), and is discharged into atmosphere by chimney (9).Meanwhile, cooling medium enters pipe (10) through cooling medium and enters precooler (5), cooling medium absorbs flue gas heat by shower or heat exchange element (11) therein and heats up into hot cooling medium, and hot cooling medium is discharged via hot cooling medium passing away (12); On the other hand, sea water pump (13) advances seawater pipe (14) input absorber (7) with the natural sea-water that extracts through absorber, and seawater sprays the flue gas that flows through and absorbs SO in the flue gas in absorber
2, the absorber drainage channel (15) from absorber (7) flows to quality recovery device (16) then, in the quality recovery device draining quality recovery is entered the nature marine site after the requirement of satisfying environmental standard.
It is as follows that the utility model is described in further detail in conjunction with the embodiments.
Expression the utility model embodiment illustrated in fig. 2 is made of two cavitys and the structure when using the fountain precooler, include: one, precooler (5) cavity, two, exhaust gases passes (6), three, absorber (7) cavity, four, hot cooling medium passing away (12); Five, absorber drainage channel (15).One end of precooler (5) cavity is associated with flue gas and enters pipe (4), and the other end has exhaust gases passes (6); One end of absorber (7) cavity is exhaust gases passes (6), and smoke outlet tube (8) is arranged at top.One end of precooler (5) cavity also is associated with cooling medium and enters pipe (10), wherein is provided with shower (11), and the other end has hot cooling medium passing away (12); The upper end of absorber (7) cavity has absorber to advance seawater pipe (14), and there is absorber drainage channel (15) lower end, and absorber can be absorber towers such as material filling type, sieve-board type or open-core type.
Precooler and absorber can also be made of tower body independently, and the two has exhaust gases passes to connect.Fig. 3 represents that the utility model is made of two independent tower bodies and the structure when using the fountain precooler.
Precooler can be made of heat exchange element.Fig. 4 represents that the utility model is made of two independent tower bodies and the structure when using heat exchange element formula precooler.
Precooler can be located at the absorber below and be arranged at same tower body with absorber.Fig. 5 represents that the utility model is located at absorber below by precooler and structure when being arranged at same tower body and using heat exchange element formula precooler with absorber.
Advantage of the present utility model is, cooling medium discharges separately, thereby guaranteed the high desulfurization efficiency of desulphurization system, particularly precooler and absorber are divided into two cavitys or two structures that tower body is provided with shown in Fig. 2, Fig. 3, Fig. 4, the embodiment, when having high desulfurization efficiency, also have the advantage that reduces operating cost and cost significantly.The material of the utility model device can be metal or cement or organic material structure.
Claims (6)
1, a kind of seawater method apparatus for absorbing SO 2, it comprises flue gas precooler and sulfur dioxide absorber, it is characterized in that, precooler discharge cooling medium and absorber draining have passing away separately.
2, device according to claim 1 is characterized in that, flue gas precooler and sulfur dioxide absorber are made of two cavitys, between two cavitys exhaust gases passes are arranged.
3, device according to claim 1 is characterized in that, flue gas precooler and sulfur dioxide absorber are made of two independent tower bodies, has exhaust gases passes to connect between two tower bodies.
4, device according to claim 1 is characterized in that, precooler can be that flue gas enters pipe self.
5, device according to claim 1 is characterized in that, precooler can be arranged at same tower body with the sulfur dioxide absorber.
6, device according to claim 1 is characterized in that, precooler can be shower type or heat exchange element formula structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98235799 CN2346494Y (en) | 1998-05-22 | 1998-05-22 | Smoke, SO2 absorbing appts, by seawater process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98235799 CN2346494Y (en) | 1998-05-22 | 1998-05-22 | Smoke, SO2 absorbing appts, by seawater process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2346494Y true CN2346494Y (en) | 1999-11-03 |
Family
ID=33984000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98235799 Expired - Fee Related CN2346494Y (en) | 1998-05-22 | 1998-05-22 | Smoke, SO2 absorbing appts, by seawater process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2346494Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102112207A (en) * | 2008-06-13 | 2011-06-29 | 彭斯干 | Washing device and washing method for marine exhaust flue gases |
| CN105289245A (en) * | 2015-10-18 | 2016-02-03 | 彭斯干 | Boiler exhaust smoke and seawater filler washing desulfurization method and washing device |
| CN105536484A (en) * | 2016-02-01 | 2016-05-04 | 西安交通大学 | Pollutant pretreating tower condensing based on flue gas |
| US9757686B2 (en) | 2008-06-13 | 2017-09-12 | Sigan Peng | Ship flue gas scrubbing apparatus and method |
-
1998
- 1998-05-22 CN CN 98235799 patent/CN2346494Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102112207A (en) * | 2008-06-13 | 2011-06-29 | 彭斯干 | Washing device and washing method for marine exhaust flue gases |
| CN102112207B (en) * | 2008-06-13 | 2013-06-19 | 武汉晶源环境工程有限公司 | Washing device and washing method for marine exhaust flue gases |
| US8500893B2 (en) | 2008-06-13 | 2013-08-06 | Sigan Peng | Ship flue gas scrubbing equipment and method |
| US9757686B2 (en) | 2008-06-13 | 2017-09-12 | Sigan Peng | Ship flue gas scrubbing apparatus and method |
| CN105289245A (en) * | 2015-10-18 | 2016-02-03 | 彭斯干 | Boiler exhaust smoke and seawater filler washing desulfurization method and washing device |
| WO2017067087A1 (en) * | 2015-10-18 | 2017-04-27 | 彭斯干 | Method of venting smoke and cleaning and desulfurizing furnace using sea water and filler and cleaning device utilizing same |
| CN105536484A (en) * | 2016-02-01 | 2016-05-04 | 西安交通大学 | Pollutant pretreating tower condensing based on flue gas |
| CN105536484B (en) * | 2016-02-01 | 2018-08-21 | 西安交通大学 | A kind of pollutant pre-corrosion tower based on flue gas condensing |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |