CN201337883Y - Smoke gas desulfurization device of circulating fluid bed - Google Patents
Smoke gas desulfurization device of circulating fluid bed Download PDFInfo
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- CN201337883Y CN201337883Y CNU2009201124792U CN200920112479U CN201337883Y CN 201337883 Y CN201337883 Y CN 201337883Y CN U2009201124792 U CNU2009201124792 U CN U2009201124792U CN 200920112479 U CN200920112479 U CN 200920112479U CN 201337883 Y CN201337883 Y CN 201337883Y
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- circulating fluid
- fluid bed
- flue
- gas
- bed reactor
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Abstract
The utility model relates to a smoke gas desulfurization device of a circulating fluid bed, which comprises a circulating fluid bed reactor. A pulse filter which is communicated with smoke gas is arranged at the upper end of the circulating fluid bed reactor, a mixing chamber of a bed material is connected with the pulse filter, the bed material enters from the bottom part of the circulating fluid bed reactor, a dust remover with a chimney is arranged at the upper side of the circulating fluid bed reactor, and a granule controller and a dust bin are arranged at the lower end of the circulating fluid bed reactor; the smoke gas forms carbon black granules after being filtered by the pulse filter, and the bed material is mixed by the carbon black granules adding with an absorbing agent and lime in the mixing chamber of the bed material; a Venturi device is arranged at the bottom part of the circulating fluid bed reactor, a water spraying device is arranged at an opening expansion zone of the Venturi device, and one side of the granule controller is communicated with the Venturi device. The smoke gas desulfurization device has the advantages of reasonable structure, high utilization rate of the bed material, high desulfurization efficiency, good economic benefits and small area occupying.
Description
Technical field
The utility model relates to a kind of flue gas desulfurization and dedusting technical field, especially relates to a kind of circulating fluid bed flue-gas desulfurizing device device.
Background technology
Described desulfurizer is a kind of device that is used for removing sulfur dioxide in flue gas and sulfur trioxide specially.It is to realize by the interaction between flue gas and desulfurization medium.At present, the flue gas desulfur device and the process of multiple pattern arranged both at home and abroad, and described flue gas desulfur device and process successfully have been applied to practice.Wherein there is the utility model patent of China Patent No. 200610117516.X to disclose a kind of " sintering smoke wet method sulphur removing and dust removing technology ", this sinter fume cools off defluorinate earlier after supercharging, HF in the flue gas is captured and with below the cigarette temperature drop to 80 ℃ by alkali lye; Flue gas enters the high-efficiency desulfurization absorption tower subsequently, by the effect of swirl-flow devices in the air jet pipe in the tower, flue gas is spun in the slurries pond at a high speed, and flue gas is broken and fully mix with slurries in slurries, finishes the desulfurization and dedusting process; Clean flue gas after the demist is discharged from chimney the heat back by the sintering waste heat steam again.
Utility model patent " sintering smoke wet method sulphur removing and dust removing technology " advantage of this China Patent No. 200610117516.X is to have higher desulfuration efficiency and efficiency of dust collection, cool off the thermal safety that has guaranteed tower that is provided with of defluorinate device, and reduced the extent of corrosion of tower inside; Next is a movement-less part in the described absorption tower, and gas-liquid contact effect is better, thereby has improved the stability of system's operation.
Yet, process equipments such as wastewater treatment equipment will be set in the wet desulfurization system of the utility model patent of above-mentioned China Patent No. 200610117516.X " sintering smoke wet method sulphur removing and dust removing technology ", its structure with move all more complicated, and occupation of land face is bigger.
The utility model content
Technical problem to be solved in the utility model is the situation at prior art, and a kind of rational in infrastructure and bed material utilization rate and desulfuration efficiency is higher and floor space is less circulating fluid bed flue-gas desulfurizing device are provided.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of circulating fluid bed flue-gas desulfurizing device, comprise the bed material mixing chamber that is connected with described flue gas, this flue gas is connected with circulating fluid bed reactor respectively with described bed material, this circulating fluid bed reactor upside is provided with fiber bag precipitator, this fiber bag precipitator one side is communicated with chimney, this fiber bag precipitator lower end connects a particle controller, this particle controller lower end links to each other with grey storehouse, it is characterized in that: be provided with pulse filter between described flue gas and the described bed material mixing chamber; Described bed material be by described flue gas filter the carbon black granules that the back forms through described pulse filter and add adsorbent with lime after, mixing composition in described bed material mixing chamber.
Owing to adopt pulse filter to smoke filtration, the carbon black material makes its bed material that becomes recirculating fluidized bed, the Sox that reciprocally adsorbs in the flue gas capable of circulation, HCL, HF, CO2 gas in the recovery flue gas; Thereby utilization rate expected by bed and desulfuration efficiency is higher, floor space is less again.
Described bed material can be connected with described circulating fluid bed reactor bottom.Its effect is that the carbon black material that reclaims in the flue gas obtains fully reaction in circulating fluid bed reactor.
Described flue gas and described bed material weight ratio can be established as: described flue gas weight is less than or equals per 1 kilogram of supporting described bed material weight is 0.5 kilogram.Can obtain desulfuration efficiency preferably like this.
Described pulse filter upside is provided with a pernicious gas passage, and this pernicious gas passage is connected with described circulating fluid bed reactor bottom.Then pernicious gas by circulating fluid bed reactor after deduster discharge from chimney.
The bottom of described circulating fluid bed reactor can be provided with Venturi, and this Venturi is made up of enlarging district, bottle-neck section and region of convergence; This enlarging district is provided with water injector.Its effect is to spray into atomized water with described bed material of humidification and circulation desulfurization thing hybrid particles surface, and makes described flue gas create the good needed temperature of fast chemical reaction; The flue gas of smoke evacuation does not need to heat again.
Described particle controller one side can be connected with described Venturi.Its effect is can catch part circulation desulfurization thing without fully reaction in circulating fluid bed reactor to return circulating fluid bed reactor continuation reaction by the particle controller again from fiber bag precipitator, to increase economic efficiency.
Described pernicious gas passage can enter described circulating fluid bed reactor by blower fan.
The cloth bag of described fiber bag precipitator is installed in the cyclone separator outlet of described circulating fluid bed reactor.
Material that described cloth bag uses is the lightening fire resistant aromatic polyamide.Its objective is applicable to than the lower operating temperature of glass fibre spinning blanket cloth bag commonly used.
The utility model is owing to adopt pulse filter to smoke filtration and after reclaiming in the flue gas carbon black material and desulfurizing agent mixing, make it become the bed material of recirculating fluidized bed, this material is at NOx, SOx, HCL, the HF etc. that can adsorb circularly in the circulating fluid bed reactor in the flue gas, and it is recycling that the bed material is participated in fully; Compared with prior art, its advantage is rational in infrastructure, a bed material utilization rate and desulfuration efficiency is higher, good in economic efficiency, floor space is less.
Description of drawings
Fig. 1 is a system architecture schematic diagram of the present utility model;
The specific embodiment
Below in conjunction with accompanying drawing embodiment the utility model circulating fluid bed flue-gas desulfurizing device is described in further detail.
As shown in Figure 1, it comprises a circulating fluid bed reactor 3, the upper end of this circulating fluid bed reactor 3 is provided with a pulse filter 1 that is connected with flue gas 11, and this pulse filter 1 connects the mixing chamber 2 of a sorbent bed material 23, and these material 23 bottoms from circulating fluid bed reactor 3 enter.
This pulse filter 1 upside is provided with a pernicious gas passage 12, and this pernicious gas passage 12 is connected with the bottom of circulating fluid bed reactor 3 by a blower fan 13.
The structure of pulse filter 1 and function are that the advance mouth of flue gas 11 from pulse filter entered, by filter core wherein, dust is attached on this filter core by collection, flue gas after being purified 11 is passed this filter core and is entered a pure qi (oxygen) case, discharge from the outlet flue of pulse filter, ash on the described filter core sends instruction by control instrument, triggers each control valve in order, adopts the instantaneous ground warp pulse tube ejection of compressed air; Described filter core sharply expands under air-flow moment acting in opposition, makes this cartridge surface dust releasing, and filter core obtains regeneration, and the carbon powder dust that is fallen clearly falls into a material mixing chamber 2.Failing the pernicious gas of filtering again in the flue gas 11 then enters circulating fluid bed reactor 3 through pernicious gas passage and blower fan, gets rid of through deduster 6 and chimney 11 again.
This sorbent bed material 23 filters the carbon black granules that the back forms by flue gas 11 through pulse filters 1 and adds adsorbent 21 and mixes in bed material mixing chamber 2 with lime 22 and form.Active carbon is added in the sinter fume steam of sorbent bed material 23 in circulating fluid bed reactor 3 and is used for absorption of N Ox, SOx, HCL, HF etc.
In order to obtain desulfuration efficiency preferably, it is 0.5 kilogram that flue gas and a bed material weight ratio can be chosen for that flue gas weight is less than or equals per 1 kilogram of supporting bed material weight.
The bottom of circulating fluid bed reactor 3 is provided with Venturi 31, and this Venturi 31 includes enlarging district, bottle-neck section and region of convergence; These Venturi tube 31 enlarging districts are provided with water injector 5.
Circulating fluid bed reactor 3 upsides connect a fiber bag precipitator 6 by its cyclone separator; This cloth bag is installed in the outlet of described cyclone separator, removes all particulate and active carbons in the flue gas before being used in being released to atmosphere; Material that this cloth bag uses is a kind of lightening fire resistant aromatic polyamide, its objective is to be applicable to than the lower operating temperature of glass fibre spinning blanket cloth bag commonly used (300 degree Celsius), is about 200 degree Celsius; These fiber bag precipitator 6 upsides connect a chimney 11; These deduster 6 lower ends connect a particle controller 4.
These particle controller 4 one sides are connected with circulating fluid bed reactor 3, and these particle controller 4 lower ends link to each other with the grey storehouse 7 of a band air exhauster 8.
The effect of particle controller 4 is that can to catch a part from fiber bag precipitator 6 be that active carbon enters in the circulating fluid bed reactor without the circulation desulfurization thing 41 of fully reaction in circulating fluid bed reactor, to adsorb the Sox in the flue gas circularly, HCL, HF, CO2 gas improves desulfuration efficiency.
The utility model circulating fluid bed flue-gas desulfurizing device is based on the recirculating fluidized bed principle, it by as the pulsers filter 1 of smoke filtration system, as the bed material preparation system of adsorbent bed material mixing chamber 2, circulating fluid bed reactor 3, as material reclaim the particle controller 4 of recirculating system, as the water injector 5 of fresh water (FW) system, as the deduster 6 of dust pelletizing system after the desulfurization, carry and the grey storehouse 7 and the electric control system thereof of storage system are formed as the desulfurization ash.Its technical process is as follows:
The formation carbon black granules mixed in bed material mixing chamber 2 with adsorbent 21, the lime 22 of adding and forms sorbent bed material 23 after flue gas 11 filtered through pulse filter 1 earlier, and this sorbent bed material 23 enters from the bottom of circulating fluid bed reactor 3.
High-temperature flue gas 11 and bed material 23 and the 41 abundant premixeds of the circulation desulfurization thing in particle controller 4 carry out preliminary desulphurization reaction in circulating fluid bed reactor 3; The Venturi 31 that passes through the bottom of circulating fluid bed reactor 3 then forms high velocity airs, bed material 23 is subjected to the percussion of this high velocity air with circulation desulfurization thing 41 and suspends, and makes this circulating fluid bed reactor 3 carry out sufficient desulphurization reaction of second step.
Bottle-neck section inner fluid at Venturi 31 is in fierce turbulence state, and the calcium sulfur ratio value in the circulating fluid bed reactor 3 can reach 40～50; Has very big landing speed between described bed material 23, circulation desulfurization composition granule 41 and the flue gas 11, this material 23 constantly rubs, collides and upgrade with the reaction interface of circulation desulfurization thing 41 hybrid particles, has greatly strengthened the transmission course of desulfurization chemical reaction process and heat energy.Simultaneously, discharge from the grey cinder notch 32 of circulating fluid bed reactor 3 downsides at this material 23 and the part solid lime-ash of the course of reaction of circulation desulfurization thing 41 hybrid particles.
The effect of the water injector 5 that is provided with in Venturi tube 31 enlarging districts is to spray into atomized water with described bed material of humidification and circulation desulfurization thing hybrid particles surface; Next is to make described flue gas have good desulfurization reaction temperature.
Ash-laden gas after the purification to discharge, enters fiber bag precipitator 6 from circulating fluid bed reactor 3 top sides then, discharges from chimney 14 again.
Because exhaust gas temperature is higher than about 20 ℃ of dew-point temperatures, so flue gas does not need to heat again; Simultaneously, the anti-corrosion measure that whole system need not be any.
The utility model adsorbent option its objective is organic pollutions such as absorption bioxin.The bed material adds before the Venturi tube of circulating fluid bed reactor 3, pass through Venturi tube with flue gas, form recirculating fluidized bed on Venturi tube top, make between bed material and the flue gas and bump the building at high speed mutually, friction constantly, and produce very big relative landing speed, thus greatly strengthened heat transfer, mass transfer between gas-solid, make the bed material form active carbon and remove NOx, SOx in the flue gas, gases such as HCL, HF Ji organic pollutions such as bioxin; In order to reach best reaction temperature, set up the spray cooling device in venturi throat, simultaneously to reach the needed temperature of fast chemical reaction.
The utility model characteristics are to adopt pulse filter to smoke filtration, carbon black material and desulphurizer mixing in the recovered flue gas After, make it become the bed material of recirculating fluidized bed, this material can adsorb flue gas circularly in circulating fluid bed reactor In NOx, SOx, HCL, HF gas, it is recycling that bed material is participated in fully; Desulfurizing agent is in the time of reactor Can reach more than 30 minutes, utilization rate can reach 99%, can satisfy load fluctuation in the variation of 30%～100% scope. Thereby The utility model reasonable structural arrangement, desulfuration efficiency are higher.
The utility model water spray is in order to reduce flue-gas temperature, and flue-gas temperature can be with technological operation changed condition, flue-gas temperature General control is at 120～180 ℃. Do not need water treatment system, accessory substance is also relatively less.
Claims (9)
1, a kind of circulating fluid bed flue-gas desulfurizing device, comprise the bed material mixing chamber that is connected with described flue gas, this flue gas is connected with circulating fluid bed reactor respectively with described bed material, this circulating fluid bed reactor upside is provided with fiber bag precipitator, this fiber bag precipitator one side is communicated with chimney, this fiber bag precipitator lower end connects a particle controller, this particle controller lower end links to each other with grey storehouse, it is characterized in that: be provided with pulse filter (1) between described flue gas (11) and the described bed material mixing chamber (2); Described bed material (23) filters the carbon black granules that the back forms by described flue gas (11) through described pulse filter (1) and adds adsorbent (21) and mixes in described material mixing chamber (2) with lime (22) and form.
2, circulating fluid bed flue-gas desulfurizing device according to claim 1 is characterized in that: described bed material (23) is connected with described circulating fluid bed reactor (3) bottom.
3, circulating fluid bed flue-gas desulfurizing device according to claim 1 is characterized in that: described flue gas (11) is established as with described bed material (23) weight ratio: be less than or equal per 1 kilogram of described flue gas (11) weight to be matched in described bed material (23) weight be 0.5 kilogram.
4, circulating fluid bed flue-gas desulfurizing device according to claim 1, it is characterized in that: described pulse filter (1) upside is provided with a pernicious gas passage (12), and this pernicious gas passage (12) is connected with described circulating fluid bed reactor (3) bottom.
5, circulating fluid bed flue-gas desulfurizing device according to claim 4 is characterized in that: the bottom of described circulating fluid bed reactor (3) is provided with Venturi (31), and this Venturi (31) is made up of enlarging district, bottle-neck section and region of convergence; This enlarging district is provided with water injector (5).
6, circulating fluid bed flue-gas desulfurizing device according to claim 1 or 5, it is characterized in that: described particle controller (4) one sides are connected with described Venturi (31).
7, circulating fluid bed flue-gas desulfurizing device according to claim 4 is characterized in that: described pernicious gas passage (12) enters described circulating fluid bed reactor (3) by blower fan (13).
8, circulating fluid bed flue-gas desulfurizing device according to claim 1 is characterized in that: the cloth bag of described fiber bag precipitator (6) is installed in the cyclone separator outlet of described circulating fluid bed reactor (3).
9, circulating fluid bed flue-gas desulfurizing device according to claim 8 is characterized in that: material that described cloth bag uses is the lightening fire resistant aromatic polyamide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201124792U CN201337883Y (en) | 2009-01-12 | 2009-01-12 | Smoke gas desulfurization device of circulating fluid bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201124792U CN201337883Y (en) | 2009-01-12 | 2009-01-12 | Smoke gas desulfurization device of circulating fluid bed |
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| Publication Number | Publication Date |
|---|---|
| CN201337883Y true CN201337883Y (en) | 2009-11-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2009201124792U Expired - Lifetime CN201337883Y (en) | 2009-01-12 | 2009-01-12 | Smoke gas desulfurization device of circulating fluid bed |
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| CN (1) | CN201337883Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101462022B (en) * | 2009-01-12 | 2011-06-29 | 宁波怡诺能源科技有限公司 | Circulating fluid bed flue-gas desulfurizing device |
| CN102580517A (en) * | 2011-01-18 | 2012-07-18 | 刘上光 | Fume desulfurization system and method by adopting dried alkali electrostatic spraying and fume humidifying cooling method |
-
2009
- 2009-01-12 CN CNU2009201124792U patent/CN201337883Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101462022B (en) * | 2009-01-12 | 2011-06-29 | 宁波怡诺能源科技有限公司 | Circulating fluid bed flue-gas desulfurizing device |
| CN102580517A (en) * | 2011-01-18 | 2012-07-18 | 刘上光 | Fume desulfurization system and method by adopting dried alkali electrostatic spraying and fume humidifying cooling method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20091104 Effective date of abandoning: 20090112 |