CN102274685B - Smoke wet desulphurization cooling device - Google Patents
Smoke wet desulphurization cooling device Download PDFInfo
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- CN102274685B CN102274685B CN 201110152437 CN201110152437A CN102274685B CN 102274685 B CN102274685 B CN 102274685B CN 201110152437 CN201110152437 CN 201110152437 CN 201110152437 A CN201110152437 A CN 201110152437A CN 102274685 B CN102274685 B CN 102274685B
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- cooling
- base plate
- cooling system
- baseboard
- cooling device
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- 238000001816 cooling Methods 0.000 title claims abstract description 138
- 239000000779 smoke Substances 0.000 title claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000002002 slurry Substances 0.000 claims description 19
- 239000007921 spray Substances 0.000 claims description 11
- 239000000443 aerosol Substances 0.000 claims description 10
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 8
- 239000012809 cooling fluid Substances 0.000 claims description 8
- 239000003546 flue gas Substances 0.000 claims description 8
- 238000010521 absorption reaction Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 230000002411 adverse Effects 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 230000008021 deposition Effects 0.000 claims description 3
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 230000007774 longterm Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 3
- 239000000110 cooling liquid Substances 0.000 abstract 2
- 238000007599 discharging Methods 0.000 abstract 2
- 210000004911 serous fluid Anatomy 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000002585 base Substances 0.000 description 53
- 239000013505 freshwater Substances 0.000 description 8
- 239000002699 waste material Substances 0.000 description 7
- 235000019738 Limestone Nutrition 0.000 description 5
- 239000003513 alkali Substances 0.000 description 5
- 238000010276 construction Methods 0.000 description 5
- 239000006028 limestone Substances 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- 239000010440 gypsum Substances 0.000 description 4
- 229910052602 gypsum Inorganic materials 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- WAIPAZQMEIHHTJ-UHFFFAOYSA-N [Cr].[Co] Chemical compound [Cr].[Co] WAIPAZQMEIHHTJ-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009851 ferrous metallurgy Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The invention relates to a smoke wet desulphurization cooling device. One discharging port is shared by a first-level cooling system and a second-level cooling system and the first-level cooling system and the second-level cooling system are arranged at the rear end of a cylinder, wherein the first-level cooling system is characterized by aerial fog cooling and is composed of a plurality of spraying guns; the spraying guns are uniformly mounted on a bracket; gas/liquid sources of the spraying guns enter from the upper part and the two sides of the cylinder; the second-level cooling system is composed of a plurality of hollow conical nozzles; the hollow conical nozzles are uniformly mounted on the bracket; a cooling serous fluid enters from the upper part or the bottom part of the cylinder; a first baseboard, a second baseboard, a third baseboard, a fourth baseboard, a fifth baseboard and a sixth baseboard are arranged on the bottom part of the cylinder; all the baseboards are connected in turn; a step which is used for preventing the cooling liquid from flowing backward is formed on the first baseboard; and the third baseboard and the fifth baseboard are arranged obliquely, thereby ensuring that the cooling liquid smoothly flows to the discharging port. The smoke wet desulphurization cooling device has the advantages that the structure is simple, the manufacturing and the mounting are convenient, the arrangement is reasonable, the constructing and running costs are lowered, the real cooling effect is achieved, and the solid foundation is established for the long-term running of a desulphurization system.
Description
Technical field
The invention belongs to Ferrous Metallurgy sintering smoke wet method sulphur technical field, particularly for the cooling device before the smoke-gas wet desulfurization.
Background technology
Cooling device before traditional sintering smoke wet method sulphur as shown in Figure 1 and Figure 2.
Cooling device shown in Figure 1 comprises one-level cooling system 12, the waste liquid outlet 13 of rinse-system 11, the barrel front end of barrel front end, secondary cooling system 14 and the cooling device base plate 15 of cylinder back-end.The weakness of this kind cooling device is that the waste liquid that one-level cooling (lime stone slurry) and secondary cooling (fresh water (FW)) produce can not be discharged effectively, and particularly secondary cools off the impact that the waste liquid that produces still is subjected to flue gas resistance, is difficult to reflux.Through long-play, hoard a large amount of gypsum at the base plate of cooling device, stop up outlet.For example a certain purpose cooling device is because of the gypsum overheap, the cooling device base plate cracking that is crushed out of shape that can't bear the heavy load, and corrosion-resistant lining material Hastelloy C alloys-276 lost efficacy simultaneously, brought about great losses to project.
Cooling device shown in Figure 2 comprises the rinse-system 21 of barrel front end, the one-level cooling system 22 of barrel front end, secondary cooling system 24, cooling device base plate 25 and the secondary cooling outlet 26 that one-level is cooled off outlet 23, cylinder back-end.This kind cooling device has solved at base plate hoards a large amount of gypsum problems, but too loaded down with trivial details, and two place's outlets need not be set.
Cooling device illustrated in figures 1 and 2 all is provided with the rinse- system 11,21 of barrel front end, and the one- level cooling system 12,22 of barrel front end all is to absorb cooling with alkali lye (being generally lime stone slurry) simultaneously.Because it is very high to enter the flue-gas temperature of barrel front end, on average is about 120 ℃～150 ℃.Under such high temperature, the lime stone slurry fouling that is cured very soon, and then stop up the one-level cooling jet, cause the one-level cooling failure.Only depending on secondary cooling flue-gas temperature to be reduced to below 70 ℃ (be higher than 70 ℃ can scaling loss absorption tower internals), need use a large amount of fresh water (FW)s, so namely waste energy and can produce a large amount of waste water, is to be uneconomical again not environmental protection.
Therefore, be necessary that developing a kind of smoke wet desulphurization cooling device in the art solves the problems referred to above: the one, the cooling device base plate must not be hoarded a large amount of gypsum; The 2nd, the one-level cooling system must not stop up inefficacy, guarantees to reduce simultaneously operating cost through after the I and II cooling flue-gas temperature being reduced to below 70 ℃.
Summary of the invention
Task of the present invention provides a kind of smoke wet desulphurization cooling device, it has solved the existing problem of above-mentioned prior art, cancellation is arranged on the rinse-system of barrel front end, guarantee to reduce simultaneously equipment construction cost and operating cost through after the I and II cooling flue-gas temperature being reduced to below 70 ℃.
Technical solution of the present invention is as follows:
A kind of smoke wet desulphurization cooling device comprises cylindrical shell, one-level cooling system and secondary cooling system, and described one-level cooling system and secondary cooling system only arrange place's outlet, and are arranged on cylinder back-end;
Described one-level cooling system is the aerosol cooling, some spray gun is made of, and spray gun is rack-mount equably, and the gas of spray gun, liquid source enter from top and the both sides of cylindrical shell;
Described secondary cooling system is comprised of several hollow cone nozzles, and the hollow cone nozzle is rack-mount equably, and cool slurry enters from cylindrical shell top or bottom;
Described cylinder body bottom arranges the first base plate, the second base plate, the 3rd base plate, the 4th base plate, the 5th base plate and the 6th base plate, and each base plate is linked in sequence; Wherein: the first base plate is provided with the step that prevents that cooling fluid from pouring in down a chimney, the second base plate and the 3rd base plate are to arrange for the ease of cooling holder is installed, the 3rd base plate and the 5th base plate are arranged to skewed to guarantee that cooling fluid flow to outlet smoothly, the 6th base plate also is provided with step and stops up tower internals to prevent a large amount of slurries from entering the absorption tower plenum chamber, and the shoulder height of the 6th base plate is lower than the shoulder height of the first base plate.
Described cool slurry enters from cylinder body bottom and is the best, in case grouting liquid deposition is stopped up cooling line.
The material of described hollow cone nozzle adopts carborundum.
The flow direction and the flue gas of the aerosol cooling of described one-level cooling system are equidirectional, i.e. following current cooling.
The cooling direction of the cool slurry of described secondary cooling system is the following current cooling, or is the adverse current cooling.
Smoke wet desulphurization cooling device of the present invention has following technical characterstic:
1, the I and II cooling system of cooling device only arranges place's outlet, and is arranged on cylinder back-end.The present invention does not arrange outlet in barrel front end, makes device structure succinct, reduces equipment construction cost.
2, for preventing alkali lye plug nozzle under the condition of high temperature, the cooling of aerosol spray gun is adopted in the one-level cooling, and the secondary cooling adopts alkali lye (being generally lime stone slurry) to absorb cooling.The aerosol cooling namely adopts compressed air and fresh water (FW) to mix by a certain percentage, and through the extremely strong lance ejection of atomizing effect, aerosol evenly fills the air whole cooling device cross section.
3, because the one-level cooling system adopts the cooling of aerosol spray gun, it not only plays cooling effect, can also the internal face of cooling device effectively be washed, therefore cancellation is arranged on the rinse-system of barrel front end, is intended to simplified structure, reduces and builds and operating cost.
Smoke wet desulphurization cooling device of the present invention is simple for structure to be understood, fabrication and installation are convenient, and connection and reasonable arrangement has reduced construction and operating cost, has really played cooling effect, for the desulphurization system long-term operation has been established sturdy basis.
Description of drawings
Fig. 1 is the schematic diagram of the cooling device before traditional a kind of sintering smoke wet method sulphur.
Fig. 2 is the schematic diagram of the cooling device before the traditional another kind of sintering smoke wet method sulphur.
Fig. 3 is the structural representation of a kind of smoke wet desulphurization cooling device of the present invention.
Reference numeral:
1 is the first base plate, and 2 is the second base plate, and 3 is the one-level cooling system, and 4 is the 3rd base plate, and 5 is the 4th base plate, and 6 is the secondary cooling system, and 7 is the 5th base plate, and 8 are I and II cooling outlet, and 9 is the 6th base plate, and 10 is cylindrical shell;
11 is the barrel front end rinse-system, and 12 is barrel front end one-level cooling system, and 13 is the waste liquid outlet, and 14 is cylinder back-end secondary cooling system, and 15 is the cooling device base plate;
21 is the barrel front end rinse-system, and 22 is barrel front end one-level cooling system, and 23 are one-level cooling outlet, and 24 is cylinder back-end secondary cooling system, and 25 is that cooling device base plate 5,26 is secondary cooling outlet.
The specific embodiment
Referring to Fig. 3, the invention provides a kind of smoke wet desulphurization cooling device, mainly formed by cylindrical shell 10, one-level cooling system 3 and secondary cooling system 6.One-level cooling system 3 and secondary cooling system 6 only arrange place's outlet 8, and this outlet 8 is arranged on cylindrical shell 10 rear ends.
One-level cooling system 3 is made of spray gun some for the aerosol cooling, and spray gun is rack-mount equably, and the gas of spray gun (compressed air), liquid (fresh water (FW)) source can enter from top and the both sides of cylindrical shell 10.
Secondary cooling system 6 is comprised of several hollow cone nozzles, and the hollow cone nozzle is rack-mount equably, and cool slurry can enter from cylindrical shell 10 tops, also can enter from cylindrical shell 10 bottoms.For preventing cool slurry deposition obstruction cooling line, cool slurry is to enter as the best from cylinder body bottom.That the hollow cone nozzle has is wear-resisting, anticorrosion, atomizing effect is good, rated operating pressure is low and nonclogging function.The material of hollow cone nozzle generally adopts carborundum.
Cylindrical shell 10 bottoms arrange the first base plate 1, the second base plate 2, the 3rd base plate 4, the 4th base plate 5, the 5th base plate 7 and the 6th base plate 9, and each base plate is linked in sequence.Wherein: the first base plate 1 arranges and prevents the step that cooling fluid is poured in down a chimney; The second base plate 2 and the 3rd base plate 4 are to arrange for the ease of cooling holder is installed; The 3rd base plate 4 and the 5th base plate 7 are arranged to skewed, to guarantee that cooling fluid flow to outlet 8 smoothly; The 6th base plate 9 also is provided with step and stops up tower internals to prevent a large amount of slurries from entering the absorption tower plenum chamber, and the shoulder height of the 6th base plate 9 is lower than the shoulder height of the first base plate 1.
The waste liquid that the I and II cooling of smoke wet desulphurization cooling device of the present invention produces directly enters slurry pool of absorption tower by the place's outlet that is arranged on cylinder back-end, recycles as desulfurizing agent.
The flow direction and the flue gas of the aerosol cooling of one-level cooling system are equidirectional, i.e. following current cooling.The cooling alkali lye of secondary cooling system or the cooling direction of lime stone slurry can be cooled off for following current, also can be adverse current cooling, must guarantee during adverse current that alkali lye does not pour in down a chimney and damages booster fan.
The inwall of this device adopts different anti-corrosion materials anticorrosion stage by stage, and Main Basis is done the corrosion mechanism at interface, dried wet interface and wet interface and come superior, economic and practical, the safe and reliable anti-material of selection technology.
Smoke wet desulphurization cooling device of the present invention in actual applications, as shown in Figure 3, the waste liquid that I and II cooling produces is all discharged from an outlet 8, cooling device is provided with the difform base plate in six places.Wherein, the step that arranges of the first base plate 1 has played and has prevented that cooling fluid from pouring in down a chimney and then damaging the effect of booster fan; The second base plate 2 and the 4th base plate 5 are to arrange for the ease of cooling holder is installed; The 3rd base plate 4 and the 5th base plate 7 are provided with certain angle of inclination, to guarantee that cooling fluid flow to outlet 8 smoothly; The step that the 6th base plate 9 arranges is to prevent that a large amount of slurries from entering the absorption tower plenum chamber and stopping up tower internals; The shoulder height of the first base plate 1 must be higher than the shoulder height of the 6th base plate 9.
Can directly design, purchase, construct and install by the present invention for newly-built smoke wet desulphurization cooling device.Also can adopt technology of the present invention for built project, but should take full advantage of existing cooling device structure, comprise its supporting construction, rational Application the present invention.Simultaneously, intensity, rigidity and the stability of tackling existing cooling device are adjusted.
In sum, smoke wet desulphurization cooling device of the present invention is simple for structure to be understood, fabrication and installation are convenient, and connection and reasonable arrangement has reduced construction and operating cost, has really played cooling effect, for the desulphurization system long-term operation has been established sturdy basis.
Certainly, those skilled in the art in the art will be appreciated that, above-described embodiment only is that the present invention is described, and be not as limitation of the invention, as long as in connotation scope of the present invention, all will drop in the scope of claim of the present invention the variation of above-described embodiment, modification etc.
Claims (5)
1. a smoke wet desulphurization cooling device comprises cylindrical shell, one-level cooling system and secondary cooling system, it is characterized in that, described one-level cooling system and secondary cooling system only arrange place's outlet, and are arranged on cylinder back-end;
Described one-level cooling system is the aerosol cooling, some spray gun is made of, and spray gun is rack-mount equably, and the gas of spray gun, liquid source enter from top and the both sides of cylindrical shell;
Described secondary cooling system is comprised of several hollow cone nozzles, and the hollow cone nozzle is rack-mount equably, and cool slurry enters from cylindrical shell top or bottom;
Described cylinder body bottom arranges the first base plate, the second base plate, the 3rd base plate, the 4th base plate, the 5th base plate and the 6th base plate, and each base plate is linked in sequence; Wherein: the first base plate is provided with the step that prevents that cooling fluid from pouring in down a chimney, the second base plate and the 4th base plate are to arrange for the ease of cooling holder is installed, the 3rd base plate and the 5th base plate are arranged to skewed to guarantee that cooling fluid flow to outlet smoothly, the 6th base plate also is provided with step and stops up tower internals to prevent a large amount of slurries from entering the absorption tower plenum chamber, and the shoulder height of the 6th base plate is lower than the shoulder height of the first base plate.
2. smoke wet desulphurization cooling device according to claim 1 is characterized in that, described cool slurry enters from cylinder body bottom and is the best, in case grouting liquid deposition is stopped up cooling line.
3. smoke wet desulphurization cooling device according to claim 1 is characterized in that, the material of described hollow cone nozzle adopts carborundum.
4. smoke wet desulphurization cooling device according to claim 1 is characterized in that, the flow direction and the flue gas of the aerosol cooling of described one-level cooling system are equidirectional, i.e. following current cooling.
5. smoke wet desulphurization cooling device according to claim 1 is characterized in that, the cooling direction of the cool slurry of described secondary cooling system is the following current cooling, or is the adverse current cooling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110152437 CN102274685B (en) | 2011-06-08 | 2011-06-08 | Smoke wet desulphurization cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110152437 CN102274685B (en) | 2011-06-08 | 2011-06-08 | Smoke wet desulphurization cooling device |
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| Publication Number | Publication Date |
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| CN102274685A CN102274685A (en) | 2011-12-14 |
| CN102274685B true CN102274685B (en) | 2013-04-10 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2547384Y (en) * | 2002-05-18 | 2003-04-30 | 昆明理工大学 | Smoke flash cooling and purifying tower |
| EP1862211A1 (en) * | 2001-10-17 | 2007-12-05 | Mitsubishi Heavy Industries, Ltd. | Flue gaz desulfurization apparatus, flue gas desulfurization system |
| CN101168119A (en) * | 2006-10-25 | 2008-04-30 | 宝山钢铁股份有限公司 | Cooling defluorinating device before smoke wet method sulphur removing |
| CN201244440Y (en) * | 2008-08-19 | 2009-05-27 | 陈玉乐 | Accident chiller for flue-gas desulfurizing device |
| CN101762199A (en) * | 2010-01-07 | 2010-06-30 | 上海吴泾第二发电有限责任公司 | Heat-transfer pipe of flue gas cooler |
-
2011
- 2011-06-08 CN CN 201110152437 patent/CN102274685B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1862211A1 (en) * | 2001-10-17 | 2007-12-05 | Mitsubishi Heavy Industries, Ltd. | Flue gaz desulfurization apparatus, flue gas desulfurization system |
| CN2547384Y (en) * | 2002-05-18 | 2003-04-30 | 昆明理工大学 | Smoke flash cooling and purifying tower |
| CN101168119A (en) * | 2006-10-25 | 2008-04-30 | 宝山钢铁股份有限公司 | Cooling defluorinating device before smoke wet method sulphur removing |
| CN201244440Y (en) * | 2008-08-19 | 2009-05-27 | 陈玉乐 | Accident chiller for flue-gas desulfurizing device |
| CN101762199A (en) * | 2010-01-07 | 2010-06-30 | 上海吴泾第二发电有限责任公司 | Heat-transfer pipe of flue gas cooler |
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| Publication number | Publication date |
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| CN102274685A (en) | 2011-12-14 |
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