CN104959006A - Treatment tower for flue gas from boilers - Google Patents
Treatment tower for flue gas from boilers Download PDFInfo
- Publication number
- CN104959006A CN104959006A CN201510337004.3A CN201510337004A CN104959006A CN 104959006 A CN104959006 A CN 104959006A CN 201510337004 A CN201510337004 A CN 201510337004A CN 104959006 A CN104959006 A CN 104959006A
- Authority
- CN
- China
- Prior art keywords
- filter screen
- tower
- flue gas
- tower body
- sulfur dioxide
- 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.)
- Granted
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 239000003546 flue gas Substances 0.000 title claims abstract description 17
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 235000014171 carbonated beverage Nutrition 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 10
- 239000000779 smoke Substances 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 6
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 5
- 230000002745 absorbent Effects 0.000 claims description 3
- 239000002250 absorbent Substances 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 2
- 239000007921 spray Substances 0.000 abstract description 4
- 239000002912 waste gas Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract 2
- 238000003915 air pollution Methods 0.000 abstract 1
- 239000003500 flue dust Substances 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 229960004424 carbon dioxide Drugs 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 239000012982 microporous membrane Substances 0.000 description 1
- 238000011045 prefiltration Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The invention discloses a treatment tower for flue gas from boilers, and belongs to the technical field of treatment equipment for waste gas. The treatment tower comprises a tower. A flue gas inlet, a flue gas outlet and a liquid outlet are formed in the tower, a plurality of heat absorbing tube stacks, a suspended particle filter screen, a sulfur dioxide filter screen and spray nozzles are arranged in the tower, the flue gas can flow in the tower in a retracing manner under the effects of the heat absorbing tube stacks, the suspended particle filter screen and the sulfur dioxide filter screen are arranged to form layers, and the spray nozzles are positioned below the sulfur dioxide filter screen, are arranged on the side walls of the tower, are communicated with a liquid delivery pipeline and face the inside of the tower; the heat absorbing tube stacks are communicated with a circulating pipeline via water inlets and steam and water outlets of the heat absorbing tube stacks, and the circulating pipeline is arranged on the outside of the tower and is connected with a pump and a steam and water separator. The treatment tower has the advantage that the problem of air pollution due to the fact that flue gas from existing boilers is directly exhausted to the air can be solved by the aid of the treatment tower.
Description
Technical field
The present invention relates to waste gas treatment equipment technical field, especially a kind for the treatment of column for boiler smoke.
Background technology
Boiler is the heat energy utilizing fuel or other energy, water or dielectric heating, export the plant equipment that heat energy supplies people's production and living needs, what in its production process of existing boiler, its fuel combustion produced contains flue dust, the flue gas of sulfur dioxide and carbon dioxide etc. is all directly be disposed in air by chimney, its exhaust gas temperature is generally not less than 180 DEG C, reach as high as 250 DEG C, this high-temperature flue gas discharge not only causes a large amount of thermal waste, the atmosphere pollution that simultaneously also to cause with flue dust and sulfur dioxide be representative, result shows after deliberation, the concentration of Sulfur Dioxide In The Atmosphere often increases by 1 times, general mortality rate increases 1l%, TSP concentration often increases by 1 times, and general mortality rate increases by 4%, and the excessive emissions of carbon dioxide can cause global warming phenomenon, therefore a kind for the treatment of apparatus of convenient and practical boiler smoke is badly in need of.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of boiler smoke treating column, and this treating column can solve that existing boiler smoke is in line causes air-polluting problem in the air.
In order to solve the problem, the technical solution adopted in the present invention is: this boiler smoke treating column, comprise the tower body offering gas approach, exhanst gas outlet and liquid outlet, be provided with flue gas is turned back in described tower body suspended particulate filter screen, sulfur dioxide filter screen that multiple endothermic tube groups of flowing, level arrange in described tower body and be positioned at and be arranged on the nozzle towards tower body be communicated with on described tower body sidewall and with liquid-transport pipe-line below described sulfur dioxide filter screen; Described endothermic tube group is exported by its water inlet and carbonated drink and is connected with the circulating line of steam-water separator with the pump that is connected be arranged at outside described tower body.
In technique scheme, technical scheme can also be more specifically: the cold medium in described endothermic tube group is water, and the liquid in described liquid-transport pipe-line is ammoniacal liquor, and described suspended particulate filter screen is full glass microporous filter membrane; Described sulfur dioxide filter screen is made up of absorbent charcoal material; Described endothermic tube group is regularly arranged and the multiple U-tube communicated of connecting.
Further: steam-water separator to offer water inlet, carbonated drink import, delivery port and venthole, described carbonated drink import is connected with the carbonated drink outlet of described endothermic tube group, and described delivery port is connected with the water inlet of described pump.
Owing to have employed technique scheme, the present invention compared with prior art has following beneficial effect:
1, owing to being provided with suspended particulate filter screen and sulfur dioxide filter screen in tower body, and be provided with the nozzle connecting liquid-transport pipe-line below sulfur dioxide filter screen, during work, suspended particulate in flue dust and sulfur dioxide are first by effective filtering, then the ammoniacal liquor in liquid-transport pipe-line sprays to flue dust by the collecting carbonic anhydride in flue dust, obtaining clean gas enters in the air, free from environmental pollution, ensure that people's is healthy; And its carbonic hydroammonium generated can utilize again, has saved resource.
2, due to be provided with in tower body wherein have water and flue gas is turned back the endothermic tube group of flowing in tower body, it extends the flowing time of flue gas, makes the heat in high-temperature flue gas effectively be absorbed by U-shaped ducted water the mixture that changes steam and water into fully and flow out recycling.
3, owing to being provided with steam-water separator, steam and water export by steam-water separator respectively, and steam is used effectively, and water again enter endothermic tube group carry out heat absorption circulation, saved water resource.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing embodiment, the invention will be further described:
Boiler smoke treating column shown in Fig. 1, comprise the tower body 1 offering gas approach 1a, exhanst gas outlet 1b and liquid outlet 1c, be provided with in tower body 1 make flue gas turn back in tower body 1 flowing multiple endothermic tube groups 21, level arrange suspended particulate filter screen 6, sulfur dioxide filter screen 4 and be positioned at the nozzle 9 towards tower body 1 being arranged on below sulfur dioxide filter screen 4 and being communicated with on tower body 1 sidewall and with liquid-transport pipe-line 8; Endothermic tube group 21 is regularly arranged and the multiple U-tube communicated of connecting, endothermic tube group 21 is exported by its water inlet and carbonated drink and is connected with the circulating line 2 of steam-water separator 3 with the pump 5 that is connected be arranged at outside tower body 1, steam-water separator 3 offers water inlet 3a, carbonated drink import 3b, delivery port 3c and venthole 3d, carbonated drink import 3b is connected with the carbonated drink outlet of endothermic tube group 11, and delivery port 3c is connected with the water inlet of pump 5; Cold medium in endothermic tube group 21 is water, and the liquid in liquid-transport pipe-line 8 is ammoniacal liquor, and suspended particulate filter screen 6 is full glass microporous membrane filtration; Described sulfur dioxide filter screen 4 is made up of absorbent charcoal material.
During work, flue gas passes through suspended particulate filter screen 7 by prefiltration, the most suspended particulate of filtering, turn back in tower body again and flow to sulfur dioxide filter screen 6 place, sulfur dioxide by sulfur dioxide filter screen 6 filtering in flue gas, the ammoniacal liquor then in liquid-transport pipe-line sprays to flue dust by the collecting carbonic anhydride in flue dust; Obtaining clean gas enters in the air from exhanst gas outlet, and its carbonic hydroammonium liquid generated flows out from liquid outlet to be recycled, heat simultaneously in high-temperature flue gas is effectively absorbed cooling by U-shaped ducted water, and water changes the mixture of steam and water into and arrives steam-water separator after flowing out, steam and water export by steam-water separator respectively, steam is used effectively, and water again enter endothermic tube group carry out heat absorption circulation, saved water resource.
Claims (3)
1. a boiler smoke treating column, it is characterized in that: comprise the tower body (1) offering gas approach (1a), exhanst gas outlet (1b) and liquid outlet (1c), be provided with in described tower body (1) make flue gas turn back in described tower body (1) flowing multiple endothermic tube groups (21), level arrange suspended particulate filter screen (6), sulfur dioxide filter screen (4) and be positioned at described sulfur dioxide filter screen (4) below be arranged on the nozzle towards tower body (1) (9) be communicated with on described tower body (1) sidewall and with liquid-transport pipe-line (8); Described endothermic tube group (21) is exported by its water inlet and carbonated drink and is arranged at described tower body (1) pump (5) that is connected with outward and is connected with the circulating line (2) of steam-water separator (3).
2. boiler smoke treating column according to claim 1, is characterized in that: the cold medium in described endothermic tube group (21) is water, and the liquid in described liquid-transport pipe-line (8) is ammoniacal liquor, and described suspended particulate filter screen (6) is full glass microporous filter membrane; Described sulfur dioxide filter screen (4) is made up of absorbent charcoal material; Described endothermic tube group (21) is the regularly arranged and multiple U-tube that communicate of connecting.
3. boiler smoke treating column according to claim 1 and 2, it is characterized in that: steam-water separator (3) offers water inlet (3a), carbonated drink import (3b), delivery port (3c) and venthole (3d), described carbonated drink import (3b) is connected with the carbonated drink outlet of described endothermic tube group (11), and described delivery port (3c) is connected with the water inlet of described pump (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510337004.3A CN104959006B (en) | 2015-06-17 | 2015-06-17 | Treatment tower for flue gas from boilers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510337004.3A CN104959006B (en) | 2015-06-17 | 2015-06-17 | Treatment tower for flue gas from boilers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104959006A true CN104959006A (en) | 2015-10-07 |
| CN104959006B CN104959006B (en) | 2017-04-12 |
Family
ID=54213194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510337004.3A Active CN104959006B (en) | 2015-06-17 | 2015-06-17 | Treatment tower for flue gas from boilers |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104959006B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105435619A (en) * | 2015-11-24 | 2016-03-30 | 无锡普瑞腾传动机械有限公司 | Painting line exhaust emission system |
| CN105457438A (en) * | 2015-11-24 | 2016-04-06 | 无锡普瑞腾传动机械有限公司 | Exhaust emission system of painting line |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2467160Y (en) * | 2001-03-19 | 2001-12-26 | 赵成城 | Tri Venturi scrubbers |
| US20110262328A1 (en) * | 2010-09-13 | 2011-10-27 | Membrane Technology And Research, Inc. | Process for separating carbon dioxide from flue gas using sweep-based membrane separation and absorption steps |
| CN203155034U (en) * | 2013-04-11 | 2013-08-28 | 唐绍华 | Energy saving and smoke purifying device of boiler |
| CN204051343U (en) * | 2014-08-12 | 2014-12-31 | 泉州市银丰机械设备有限公司 | Polishing cleaner |
| CN104437041A (en) * | 2014-12-24 | 2015-03-25 | 陈学新 | Multifunctional flue gas treatment apparatus |
| CN204365080U (en) * | 2014-11-28 | 2015-06-03 | 嵩县中科孵化器有限公司 | Waste gas utilization purifier |
-
2015
- 2015-06-17 CN CN201510337004.3A patent/CN104959006B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2467160Y (en) * | 2001-03-19 | 2001-12-26 | 赵成城 | Tri Venturi scrubbers |
| US20110262328A1 (en) * | 2010-09-13 | 2011-10-27 | Membrane Technology And Research, Inc. | Process for separating carbon dioxide from flue gas using sweep-based membrane separation and absorption steps |
| CN203155034U (en) * | 2013-04-11 | 2013-08-28 | 唐绍华 | Energy saving and smoke purifying device of boiler |
| CN204051343U (en) * | 2014-08-12 | 2014-12-31 | 泉州市银丰机械设备有限公司 | Polishing cleaner |
| CN204365080U (en) * | 2014-11-28 | 2015-06-03 | 嵩县中科孵化器有限公司 | Waste gas utilization purifier |
| CN104437041A (en) * | 2014-12-24 | 2015-03-25 | 陈学新 | Multifunctional flue gas treatment apparatus |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105435619A (en) * | 2015-11-24 | 2016-03-30 | 无锡普瑞腾传动机械有限公司 | Painting line exhaust emission system |
| CN105457438A (en) * | 2015-11-24 | 2016-04-06 | 无锡普瑞腾传动机械有限公司 | Exhaust emission system of painting line |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104959006B (en) | 2017-04-12 |
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Legal Events
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20170222 Address after: No. 19 A District 545006 building the Guangxi Zhuang Autonomous Region Liuzhou Liu Dong New Area chuyang road 3 No. 151 (hi tech Zone) Applicant after: Guangxi Liuzhou Zhongjia Intellectual Property Rights Service Co., Ltd. Address before: Liuzhou Luzhai County 545609 the Guangxi Zhuang Autonomous Region Du Zhen Fu Long Cun Tun Village No. 6 Applicant before: Rong Xiuliu |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201201 Address after: 535000 office building, Qinbei economic and Technological Development Zone, zone 1, Huangma Industrial Park, Qinbei District, Qinzhou City, Guangxi Zhuang Autonomous Region Patentee after: Qinzhou real horse Asset Management Group Co., Ltd Address before: No. 19 A District 545006 building the Guangxi Zhuang Autonomous Region Liuzhou Liu Dong New Area chuyang road 3 No. 151 (hi tech Zone) Patentee before: GUANGXI LIUZHOU ZHONGJIA INTELLECTUAL PROPERTY RIGHTS SERVICE Co.,Ltd. |
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| TR01 | Transfer of patent right |