CN100518890C - Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed - Google Patents
Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed Download PDFInfo
- Publication number
- CN100518890C CN100518890C CNB2006101166141A CN200610116614A CN100518890C CN 100518890 C CN100518890 C CN 100518890C CN B2006101166141 A CNB2006101166141 A CN B2006101166141A CN 200610116614 A CN200610116614 A CN 200610116614A CN 100518890 C CN100518890 C CN 100518890C
- Authority
- CN
- China
- Prior art keywords
- tower
- desulfurization
- flue gas
- atomisation tower
- dedusting
- 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.)
- Active
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
An efficient desulfurizing-dusting technology for the circulating fluidized-bed boiler features that a desulfurizing-dusting tower by shrinkling and atomizing water is used of two-stage treating for both desulfurizing and dusting, that is, spraying lime powder in furnace for desulfurizing, shrinkling and atomizing water in the atomizing tower for desulfurizing, shrinkling and atomizing water for dusting, and using electrostatic / cloth bag duster for dusting.
Description
Technical field:
The present invention discloses a kind of efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed, belongs to the atmospheric environment protection field, is applicable to the desulfurization and the dedusting of big-and-middle-sized power station and industrial circulating fluid bed boiler.
Background technology:
CFBB (Circulating Fluidized Bed Boiler--CFBB) is because its low-temperature reinforcement aptitude to burn, have and to use inferior fuel, be easy to low-cost desulfurization, discharged nitrous oxides is low is convenient to remarkable advantages such as utilization with lime-ash, is considered to comprehensive utilization of resources and eco-friendly coal-fired thermal powerplant.Under the encouragement of national policy, obtain swift and violent development in recent years.But, in at present numerous practices, have two environmental problems to display day by day: the one,, be efficiency of combustion mainly due to the target of domestic boiler design, desulfuration efficiency does not generally reach on foreign vendor and the textbook said 90%, and great majority only are about 70～80%; The 2nd, owing to use the inferior fuel of ash-rich and spraying in a large number of desulfurization agstone, used electric cleaner efficient is not high enough, makes dust exhausting concentration and total amount all not reach requirement.
CFBB mostly adopts the method that adds lime stone and afterbody electrostatic precipitation in the stove to control the discharging of flue gas at present, but its desulfurization and dedusting effect are all low than rate, when especially using medium-high sulfur coal, are difficult to the discharge standard that reaches new.
Summary of the invention:
Technical problem to be solved by this invention is the defective that overcomes prior art, discloses a kind of efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed.
The present invention is achieved in that a kind of efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed, comprise spray agstone desulfurization in the stove, afterbody static/bag-type dust, it is characterized in that: also comprise water spraying atomization desulfurization and dedusting tower, the method of bi-level treatment is all adopted in realization desulfurization and dedusting, promptly be two-step desulfurization and two-stage dedusting, described two-step desulfurization be in the stove after the desulfurization of spray pulverized limestone back-end ductwork be provided with the spray tower activation desulfurization of spraying water; Described two-stage dedusting is to the dedusting of flue gas water spraying atomization and afterbody static/sack cleaner dedusting in the back-end ductwork spray tower.
Spray limestone desulfurization and static (cloth bag) dedusting all are ripe prior aries in the stove, and key of the present invention is that water spraying atomization desulfurization and dedusting tower (abbreviation atomisation tower) and stove interior spray agstone and deduster are combined, and realizes the low-cost high-efficiency desulfurization and dedusting.In atomisation tower, a large amount of unreacted CaO in the stove are activated into Ca (OH) by water spraying atomization
2, and under near the temperature of flue gas dew point with SO
2Continue reaction, further improve desulfuration efficiency; Simultaneously, water spraying atomization makes dust granules become big the change and weighs, and under gravity and action of centrifugal force, has considerable dust will fall at the bottom of the tower, can alleviate the burden of downstream deduster greatly, so this atomisation tower has the effect of desulfurization and dedusting simultaneously.
The invention has the beneficial effects as follows: the present invention combines water spraying atomization desulfurization and dedusting tower and in-furnace calcium spraying and deduster, realizes the low-cost high-efficiency desulfurization and dedusting.The present invention has kept the low-cost free from corrosion principal advantages of dry desulfurization, but desulfuration efficiency can reach 90～95%, near or reach the high level of wet desulphurization, be applicable to the high-efficiency desulfurization and the dedusting of big-and-middle-sized power station and industrial cycle Fluidized Bed Boiler.
Description of drawings:
Fig. 1 is water spraying atomization desulfurization and dedusting tower structure figure of the present invention;
Fig. 2 is technological process device figure of the present invention.
Among the figure: 1, uptake flue; 2, top flue gas distributor; 3, tower body; 4, spiral lifting mechanism; 5, air atomizer spray nozzle; 6, outlet damper; 7, outlet device; 8, agstone spraying system; 9, atomisation tower; 10, electrostatic precipitator; 11, burner hearth; 12, separator; 13, convection pass; 14, chimney.
The specific embodiment:
With reference to the accompanying drawings 1, the utility model atomisation tower is made up of uptake flue 1, top flue gas distributor 2, tower body 3, spiral lifting mechanism 4 air atomizer spray nozzles 5 that are connected with water pipe, the outlet plate washer 6 that is positioned at the tower bottom sidewall and outlet device 7.
With reference to the accompanying drawings 2, adopt prior art agstone spraying system 8 and static (or cloth bag) deduster 10 in conjunction with desulfurization in technology atomisation tower 9 stoves of the present invention.Atomisation tower has the effect of desulfurization and dedusting simultaneously concurrently, so group technology of the present invention realized two-step desulfurization and two-stage dedusting, can satisfy the requirement of boiler smoke discharging.In spray tower, by the flue gas distributor flue gas is divided into some strands, and air atomizer spray nozzle is placed in wherein respectively, and regulate its relative position by spiral lifting mechanism, flue gas is fully mixed and not wet wall with water smoke.When water smoke cools off flue gas, make in stove a large amount of unreacteds completely CaO activate into Ca (OH)
2, residual SO in continuation and the flue gas under near the temperature of flue gas dew point
2Reaction further improves desulfuration efficiency; Simultaneously, a large amount of water smoke makes dust granules become big the change and weighs, and under gravity and action of centrifugal force, considerable dust will be discharged from the bottom of will falling into tower, can alleviate the burden of downstream deduster greatly.The air atomizer spray nozzle that the present invention adopts is the commercially available prod, does not locate not to be described further.
On investment and operating cost economy, this programme is very superior.The front was mentioned, and the spray limestone desulfurization is most economical in all sulfur removal technologies in the circulating fluid bed boiler.In the investment, it only needs a cover lime stone to carry and injection apparatus, and efficient can reach about 70～80%.But as use higher fuel of sulfur-bearing or desulfuration efficiency to require 90% or when above, then need increase the simple and easy water spraying atomization device of a cover.Ash circulates and the cancellation flue gas heats again owing to do not establish, and the spray tower of simplification and the cost of accessory system thereof are also lower.Deduster is still used intrinsic electrostatic precipitator (also can change its last electric field into cloth bag).The gross investment of like this, new efficient desulfurizing and dust collecting process is lower than 1/3rd of wet method.Lime stone is the most cheap in the various desulfurizing agents, though the consumption of limestone amount of fluidized-bed combustion boiler is that the twice of wet method is many, but because of technology simple, energy consumption is little, does not corrode, and does not establish flue gas reheat system (GGH), there is not waste water, dry ash is easy to advantages such as processing, and operating cost is lower than 1/2nd of wet method, and reliability and life-span increase significantly.Because the circulatory system of not establishing atomisation tower bottom ash and electro-precipitating dust, this activation tower can be regarded one-level work of water sprinkling for better material moisture dust arrester as.The water smoke of ejection can increase the dirt particle and the weight of powder, under gravity and action of centrifugal force, has quite a lot of dust to land at the bottom of the tower, can significantly reduce the inlet dust concentration of electrostatic precipitator.In addition, because the reduction of flue-gas temperature and dust water capacity increase, the efficient that also helps electrostatic precipitator improves.Thereby this programme has the good result of further reduction smoke dust discharge concentration.
Technology of the present invention is applicable to and uses middle high-sulfur (S is greater than 1.0%) coal that perhaps desulfuration efficiency requires the big-and-middle-sized CFBB greater than 90%.
In sum, this circulating fluid bed boiler desulfurization dedusting new technology of combined can be with low investment and the low operating cost of dry method Reach the effect of high-efficiency desulfurization and dedusting.
Claims (3)
1. circulating fluid bed boiler desulfurization dust collecting process, comprise spray agstone desulfurization in the stove, afterbody static or bag-type dust equipment and atomisation tower (9), realize that the water spray that sprays the agstone desulfurization in the stove and be arranged on the atomisation tower (9) of back-end ductwork activates the two-step desulfurization of desulfurization and is arranged on the two-stage dedusting of the atomisation tower (9) of back-end ductwork to the dedusting of flue gas water spraying atomization and afterbody static or the dedusting of bag-type dust equipment, it is characterized in that: in the described atomisation tower (9), the top flue gas distributor (2) of cat head forms some minutes flues, flue gas is divided into some strands enters atomisation tower (9) from cat head, air atomizer spray nozzle (5) is placed in respectively in the branch flue central outlet, flue gas and water smoke are walked around the outlet damper (6) that is positioned on atomisation tower (9) the bottom column sidewall in the bottom, discharge atomisation tower (9) from the outlet device of being located on outlet damper (6) the homonymy sidewall and be positioned at the side direction of its downside (7), in atomisation tower (9), by water spraying atomization with spray lime stone in the stove after a large amount of unreacteds or unreacted completely CaO activate into Ca (OH)
2, and under near the temperature of flue gas dew point with SO
2Continue reaction.
2. circulating fluid bed boiler desulfurization dust collecting process according to claim 1, it is characterized in that: the flue gas that described top flue gas distributor (2) comes the top is divided into 3～12 strands, also is provided with spiral lifting mechanism (4) on the tube connector of the air atomizer spray nozzle (5) that each branch flue is provided with.
3. circulating fluid bed boiler desulfurization dust collecting process according to claim 1 and 2 is characterized in that: described atomisation tower (9) tower bottom sidewall is provided with outlet damper (6), and under gravity and action of centrifugal force, considerable dust lands into being discharged from the bottom of the tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101166141A CN100518890C (en) | 2006-09-28 | 2006-09-28 | Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101166141A CN100518890C (en) | 2006-09-28 | 2006-09-28 | Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1939571A CN1939571A (en) | 2007-04-04 |
| CN100518890C true CN100518890C (en) | 2009-07-29 |
Family
ID=37958258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101166141A Active CN100518890C (en) | 2006-09-28 | 2006-09-28 | Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100518890C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014110884A1 (en) * | 2013-01-18 | 2014-07-24 | 北京神雾环境能源科技集团股份有限公司 | Powdered solid fuel boiler and dry purification process system |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101537310B (en) * | 2008-03-21 | 2011-04-13 | 房靖华 | Semidry premodulation limestone-gypsum flue gas desulfurizing method |
| CN101259365B (en) * | 2008-04-25 | 2010-10-06 | 武汉凯迪电力环保有限公司 | Two-stage pre-spraying water circulating fluidized bed desulfurization technique and system thereof |
| CN101698135B (en) * | 2009-10-29 | 2012-10-03 | 北京绿源润泽环境技术有限责任公司 | Composite slaked lime desulfurizing method and device thereof |
| CN101791622B (en) * | 2010-03-17 | 2013-10-16 | 上海天顿环境工程有限公司 | Process method for converting metal magnesium slag into desulphurizer of boiler |
| CN104748144B (en) * | 2015-03-11 | 2017-01-25 | 江苏大学 | Gas-liquid coaxial ejection liquid fuel electrostatic atomization nozzle |
| CN104896494B (en) * | 2015-06-19 | 2017-07-28 | 山西大学 | A kind of waste-heat recovery device applied to dry desulfurizing process |
| CN106196023B (en) * | 2016-07-25 | 2018-01-02 | 泉州恒兴能源节能技术有限公司 | One kind cleaning burning coal CFBB |
| CN106512703B (en) * | 2016-10-31 | 2018-11-23 | 铜陵市菲力克测控技术有限公司 | Green energy conservation formula desulfurizer and its technique for flue gas purification system |
| CN106621651A (en) * | 2016-11-17 | 2017-05-10 | 成都朵猫文化传播有限公司 | Environment-friendly dust collector |
| CN106582232A (en) * | 2017-02-08 | 2017-04-26 | 江苏佳鑫环保工程有限公司 | Synergistic removal tending to zero discharge purification process and equipment for multicomponent pollutants in flue gas |
| CN108105761B (en) * | 2018-01-12 | 2024-02-13 | 哈尔滨红光锅炉总厂有限责任公司 | Ultra-low emission cooperative control method and system integration device for circulating fluidized bed boiler |
| CN113230826A (en) * | 2021-05-17 | 2021-08-10 | 安徽徽柏环保科技有限公司 | Cadmium-containing flue gas cadmium oxide heavy metal recovery and purification process |
-
2006
- 2006-09-28 CN CNB2006101166141A patent/CN100518890C/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014110884A1 (en) * | 2013-01-18 | 2014-07-24 | 北京神雾环境能源科技集团股份有限公司 | Powdered solid fuel boiler and dry purification process system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1939571A (en) | 2007-04-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100518890C (en) | Efficient desulfurizing and dust collecting process of boiler for circulating fluidized bed | |
| CN100503013C (en) | Method and system for combinedly removing SO2, NOx and Hg in coal smoke gas by using recombustion of biomass | |
| CN108636098A (en) | A kind of the minimum discharge purifier and its method of burning city domestic garbage flue gas | |
| CN202478804U (en) | Sintering machine flue gas desulphurization denitration device | |
| CN202185253U (en) | Exhaust gas purifying system for waste incineration | |
| CN101653682A (en) | Boiler-rear flue gas desulphurization and synergism device of circulating fluid bed boiler and desulphurization and synergism method | |
| CN102233230A (en) | Waste burning smoke purification process and purification system | |
| CN106582232A (en) | Synergistic removal tending to zero discharge purification process and equipment for multicomponent pollutants in flue gas | |
| CN112121614A (en) | Stable ultralow emission device and method for solid waste incineration flue gas | |
| CN106731585A (en) | A kind of coke oven flue gas dry-type desulphurization device, the dust removal integrated system and method for coke oven flue gas dry type desulfurizing | |
| CN205073877U (en) | Semidry method flue gas desulphurization device of single venturi structure | |
| CN109999574A (en) | A kind of thermopnore activated carbon adsorption method of denitration of low-sulfur flue gas | |
| CN111957197A (en) | Efficient flue gas deacidification, dioxin removal and waste heat utilization cooperative system and process | |
| CN206295800U (en) | A kind of semi-dry flue gas desulfurization device | |
| CN103301745A (en) | Cyclone separator desulfurization device | |
| CN206989168U (en) | A kind of boiler smoke minimum discharge device | |
| CN206240329U (en) | Flue gas desulfurization denitration dust-removing system | |
| CN202438257U (en) | Gas-solid circulating flue gas absorption desulfuration and dust removal device | |
| CN2813075Y (en) | Sintering machine head smoke desulfurizing device | |
| CN203671593U (en) | Internal and external cooperated pollutant removing device for boiler of flow state reconstructed circulating fluidized bed | |
| CN111085092A (en) | Desulfurization and dust removal device and desulfurization and dust removal method for gas boiler | |
| CN202224058U (en) | Desulfurization and dust removal device for sprayed supersaturation water quicklime powder | |
| CN200961867Y (en) | Circulating fluidized bed boiler desulfurizing dust-removing tower | |
| CN203355606U (en) | Cyclone separator desulfurizer | |
| CN113559692A (en) | Double-tower double-circulation semi-dry desulfurization device, process and application |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHANGHAI SINOFINN NEW ENERGY INVESTMENT CO., LTD. Free format text: FORMER NAME: SHANGHAI SINOFINN ELECTRIC ENGINEERING CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: 201203 room 5, building 3000, 513 East Dragon Road, Pudong New Area Patentee after: Sinofinn Electric Engineering Corp. Address before: 201203, Shanghai, Pudong New Area, 3000 East Road, No. 5, building 5 Patentee before: Shanghai Sinofinn Electric Engineering Co., Ltd. |