CN201423244Y - Exhaust gas desulfurization absorption tower - Google Patents

Exhaust gas desulfurization absorption tower Download PDF

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Publication number
CN201423244Y
CN201423244Y CN2009201275167U CN200920127516U CN201423244Y CN 201423244 Y CN201423244 Y CN 201423244Y CN 2009201275167 U CN2009201275167 U CN 2009201275167U CN 200920127516 U CN200920127516 U CN 200920127516U CN 201423244 Y CN201423244 Y CN 201423244Y
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CN
China
Prior art keywords
tower
absorption tower
smoke inlet
exhaust gas
tower body
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.)
Expired - Lifetime
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CN2009201275167U
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Chinese (zh)
Inventor
邓佳佳
杜云贵
余宇
吴其荣
何凡
刘艳荣
唐灿
丁开平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing University
CPI Yuanda Environmental Protection Engineering Co Ltd
Original Assignee
Chongqing University
CPI Yuanda Environmental Protection Engineering Co Ltd
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Priority to CN2009201275167U priority Critical patent/CN201423244Y/en
Application granted granted Critical
Publication of CN201423244Y publication Critical patent/CN201423244Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses an exhaust gas desulfurization absorption tower, which comprises a tower body. An exhaust gas outlet is arranged at the top part of the tower body; a slurry pool used for containing a desulphurization washing liquid is arranged at the bottom part of an inner cavity of the tower body; a washing liquid spray pipe transversely arranged inside the tower body is positioned below the exhaust gas outlet and communicated with the slurry pool through a recirculating pump; an exhaust gas inlet is arranged in the middle of the tower body and is positioned below the washing liquid spray pipe; following the downward vertical direction, at least part of the tower body adopts a structure of an outer expansion bell mouth with gradually increased ring diameters; and the exhaustgas inlet is arranged on the structure of the outer expansion bell mouth. The outer expansion bell mouth structural design adopted by the tower body eliminates the inlet inclination angle of the absorption tower, and changes an inclined exhaust gas inlet pipeline into a horizontal pipeline, thereby reducing the design difficulty, saving the material requirement of an engineering project, reducingthe pressure loss of an inlet section, and achieving the purposes of optimizing design methods and reducing the construction work cost and the operation energy consumption of the absorption tower.

Description

Fume desulfurating absorption tower
Technical field
The utility model belongs to the flue gas desulfurization device field, particularly a kind of fume desulfurating absorption tower.
Background technology
It is the country of main energy sources with coal that China is one, and coal fired power generation is one of most important approach of coal in China utilization.According to the national conditions of China, 21st century coal fired power generation will occupy an leading position.In numerous atmosphere pollutions of coal-fired fired power generating unit discharging, SO 2And dust is bigger to the harm of environment, is the major pollutants that will control.Along with the progress and the expanding economy of society, thermal power plant has been subjected to people's common concern to the pollution of atmospheric environment, and therefore effectively reducing pollutant emission is the severe challenge that China's energy field sustainable development is faced with the influence that improves environment.
At present, existing flue gas desulfurization technique comprises wet desulphurization and dry desulfurization etc.The utilization of wherein wet desulphurization technology is the most extensive.Wet process of FGD is the technological process that current 85% left and right sides large thermal power plant in the world adopts, and fume desulfurating absorption tower is its key core equipment, has obtained extensive use on engineering.The principle of wet flue gas desulfurization absorption tower is to utilize the lime stone alkaline slurry to spray from the top down, and flue gas flows from bottom to top, and lime stone slurry drops in the SO that absorbs in the dropping process in the flue gas 2, reach the SO that removes in the flue gas 2Purpose.
Characteristics such as investment is big, equipment is complicated because the wet process of FGD technology has, operating cost and specification requirement height, and in order to prevent that slurries from entering the absorption tower inlet, now Yun Hang wet flue gas desulfurization absorption tower all is designed to the inlet form to the absorption tower inner inclination, its design is complicated and can cause air-flow to dirty rather than upwards mobile, causes the pressure loss of porch excessive.The operation energy consumption that how to reduce desulfuration absorbing tower becomes the problem that presses for solution.
The utility model content
In view of this, the utility model provides a kind of fume desulfurating absorption tower, by the ingenious design of body of the tower, eliminated the inlet inclination angle on absorption tower, change the adsorption tower smoke inlet duct into level by inclination, reach the reduction design difficulty, reduce the purpose of desulfurizing tower operation energy consumption.
The purpose of this utility model provides a kind of fume desulfurating absorption tower, comprises body of the tower, and the top of described body of the tower is provided with exhanst gas outlet, and the intracavity bottom of described body of the tower is provided with the slurries pond that is used to hold the desulfurization cleaning solution; Described body of the tower inner transverse is provided with the cleaning solution shower, described cleaning solution shower is positioned at the below of exhanst gas outlet and is connected with the slurries pond by circulating pump, the middle part of described body of the tower is provided with smoke inlet, described smoke inlet is positioned at the below of cleaning solution shower, along downward vertical direction, described all or part of body of the tower adopts and encircles the structure that extends out that directly increases gradually, and described smoke inlet is arranged on described extending out on the structure.
Further, the upper extreme point of described smoke inlet and the upper end surface that extends out structure are on same level cross-sectionn, and the lower extreme point of described smoke inlet is on the same level cross-sectionn with the lower surface that extends out structure;
Further, described smoke inlet is provided with the smoke inlet pipeline of horizontal positioned;
Further, described slurries pond also is provided with the slurries stirring system, and described slurries stirring system comprises rotation slurry and the drive motors that is arranged on inside, slurries pond, and described rotation slurry connects with the drive motors axle;
Further, also comprise demister, described demister is arranged between exhanst gas outlet and the cleaning solution shower;
Further, described smoke outlet is provided with flue gas flow monitoring device I and smoke components sniffer I;
Further, described smoke inlet place is provided with flue gas flow monitoring device II and smoke components sniffer II;
Further, the described structure that extends out is horn-like hatch frame, and the described structure that extends out is connected with other parts employing rounding ofves on the body of the tower.
The beneficial effects of the utility model are: body of the tower adopts outer bell mouth expanding structural design, eliminated the inlet inclination angle on absorption tower, change the adsorption tower smoke inlet duct into level by inclination, can effectively prevent to wash slurries and enter inlet duct, reduced design difficulty, save the materials demand of engineering project, also reduced the crushing of entrance simultaneously, reached the purpose of optimizing spray type desulphurization tower method for designing, reduction construction work cost, reducing the absorption tower operation energy consumption.
Other advantages of the present utility model, target, to set forth in the following description to a certain extent with feature, and to a certain extent, based on being conspicuous to those skilled in the art, perhaps can from practice of the present utility model, obtain instruction to investigating hereinafter.Target of the present utility model and other advantages can realize and obtain by following specification and claims.
Description of drawings
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing the utility model is described in further detail, wherein:
Fig. 1 is the utility model structural representation;
Fig. 2 Fig. 1 along A-A to structural representation.
The specific embodiment
Hereinafter with reference to accompanying drawing, preferred embodiment of the present utility model is described in detail.Should be appreciated that preferred embodiment only for the utility model is described, rather than in order to limit protection domain of the present utility model.
The 1-body of the tower; The 2-exhanst gas outlet; 3-slurries pond; 4-cleaning solution shower; The 5-circulating pump; 6-extends out structure; 7-smoke inlet pipeline; 8-rotates slurry; The 9-drive motors; The 10-demister; 11-flue gas flow monitoring device I; 12-smoke components sniffer I; 13-flue gas flow monitoring device II; 14-smoke components sniffer II; The 15-smoke inlet.
Fume desulfurating absorption tower comprises body of the tower 1, and the top of body of the tower 1 is provided with exhanst gas outlet 2, and the intracavity bottom of body of the tower 1 is provided with the slurries pond 3 that is used to hold the desulfurization cleaning solution; Body of the tower 1 inner transverse is provided with cleaning solution shower 4, cleaning solution shower 4 is positioned at the below of exhanst gas outlet 2 and is connected with slurries pond 3 by circulating pump 5, the middle part of body of the tower 1 is provided with smoke inlet 15, smoke inlet 15 is positioned at the below of cleaning solution shower 4, along downward vertical direction, part body of the tower 1 adopts that the ring footpath increases gradually extends out structure 6, smoke inlet 15 is arranged on and extends out on the structure 6, wherein, the upper extreme point of smoke inlet 15 with extend out the upper end surface of structure 6 on same level cross-sectionn, the lower extreme point of smoke inlet 15 is on the same level cross-sectionn with the lower surface that extends out structure 6, and smoke inlet 15 is provided with the smoke inlet pipeline 7 of horizontal positioned.
In the present embodiment, extend out structure 6 and be horn-like hatch frame, extend out on structure 6 and the body of the tower 1 and being connected of other parts adopt the rounding off connection.
Desulfuration absorbing tower body of the tower of the present utility model adopts and extends out structure, eliminate inlet inclination angle, absorption tower, changed the absorption tower inlet into horizontal access, not only reached the purpose of avoiding slurries to enter the absorption tower inlet, and reduced design difficulty, saved the engineering project materials demand.
The slurries pond also is provided with the slurries stirring system, and the slurries stirring system comprises rotation slurry 8 and the drive motors 9 that is arranged on 3 inside, slurries pond, and rotation slurry 8 connects with 9 of drive motors.
The utility model also comprises demister 10, and demister 10 is arranged between exhanst gas outlet 2 and the cleaning solution shower 4.Exhanst gas outlet 2 is provided with flue gas flow monitoring device I 11 and smoke components sniffer I 12, the smoke inlet place is provided with flue gas flow monitoring device II 13 and smoke components sniffer II 14, be used to monitor absorption tower inlet flue gas flow, by flue gas flow monitoring device 11 and smoke components sniffer 14, can monitor SO in real time 2Concentration, according to the calcium sulfur molecule than be 1.03, the ratio of sulphur oxygen molecule is 2, the oxidation air excess coefficient is 1.9~3 principle, in time regulates lime stone slurry straying quatity and oxidation air amount.
Explanation is at last, above embodiment is only unrestricted in order to the explanation the technical solution of the utility model, although the utility model is had been described in detail with reference to preferred embodiment, those of ordinary skill in the art is to be understood that, can make amendment or be equal to replacement the technical solution of the utility model, and not breaking away from the aim and the scope of the technical program, it all should be encompassed in the middle of the claim scope of the present utility model.

Claims (8)

1. fume desulfurating absorption tower comprises body of the tower (1), and the top of described body of the tower (1) is provided with exhanst gas outlet (2), and the intracavity bottom of described body of the tower (1) is provided with the slurries pond (3) that is used to hold the desulfurization cleaning solution; Described body of the tower (1) inner transverse is provided with cleaning solution shower (4), described cleaning solution shower (4) is positioned at the below of exhanst gas outlet (2) and is connected with slurries pond (3) by circulating pump (5), the middle part of described body of the tower (1) is provided with smoke inlet (15), described smoke inlet (15) is positioned at the below of cleaning solution shower (4), it is characterized in that: along downward vertical direction, extend out structure (6) to what small part body of the tower (1) adopted that the ring footpath increases gradually, described smoke inlet (15) is arranged on described extending out on the structure (6).
2. fume desulfurating absorption tower according to claim 1, it is characterized in that: the upper extreme point of described smoke inlet (15) and the upper end surface that extends out structure (6) are on same level cross-sectionn, and the lower extreme point of described smoke inlet (15) is on the same level cross-sectionn with the lower surface that extends out structure (6).
3. fume desulfurating absorption tower according to claim 2 is characterized in that: described smoke inlet (15) is provided with the smoke inlet pipeline (7) of horizontal positioned.
4. fume desulfurating absorption tower according to claim 3, it is characterized in that: described slurries pond also is provided with the slurries stirring system, described slurries stirring system comprises that being arranged on the inner rotation in slurries pond (3) starches (8) and drive motors (9), and described rotation slurry (8) connects with drive motors (9) axle.
5. fume desulfurating absorption tower according to claim 4 is characterized in that: also comprise demister (10), described demister (10) is arranged between exhanst gas outlet (2) and the cleaning solution shower (4).
6. fume desulfurating absorption tower according to claim 5 is characterized in that: described exhanst gas outlet (2) is provided with flue gas flow monitoring device I (11) and smoke components sniffer I (12).
7. fume desulfurating absorption tower according to claim 6 is characterized in that: described smoke inlet place is provided with flue gas flow monitoring device II (13) and smoke components sniffer II (14).
8. fume desulfurating absorption tower according to claim 7 is characterized in that: the described structure (6) that extends out is horn-like hatch frame, and the described structure (6) that extends out connects with the employing rounding off that is connected that body of the tower (1) is gone up other parts.
CN2009201275167U 2009-05-31 2009-05-31 Exhaust gas desulfurization absorption tower Expired - Lifetime CN201423244Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009201275167U CN201423244Y (en) 2009-05-31 2009-05-31 Exhaust gas desulfurization absorption tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009201275167U CN201423244Y (en) 2009-05-31 2009-05-31 Exhaust gas desulfurization absorption tower

Publications (1)

Publication Number Publication Date
CN201423244Y true CN201423244Y (en) 2010-03-17

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Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102180529A (en) * 2011-03-30 2011-09-14 东南大学 L-shaped desulphurization wastewater flue gas evaporating plant
CN101564642B (en) * 2009-05-31 2011-09-28 中电投远达环保工程有限公司 Fume desulfurization absorber

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101564642B (en) * 2009-05-31 2011-09-28 中电投远达环保工程有限公司 Fume desulfurization absorber
CN102180529A (en) * 2011-03-30 2011-09-14 东南大学 L-shaped desulphurization wastewater flue gas evaporating plant
CN102180529B (en) * 2011-03-30 2012-08-22 东南大学 L-shaped desulphurization wastewater flue gas evaporating plant

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20100317

Effective date of abandoning: 20090531