CN105797531A - Method for inhibiting emission of fine particles in process of iron-ore sintering by agglomeration process - Google Patents
Method for inhibiting emission of fine particles in process of iron-ore sintering by agglomeration process Download PDFInfo
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Abstract
The invention discloses a method for inhibiting emission of fine particles in the process of iron-ore sintering by an agglomeration process and belongs to the technical field of emission reduction of pollutants in the process of iron-ore sintering. The method comprises the following steps: (1) preparing agglomeration liquid, namely uniformly mixing components such as sodium carboxymethyl cellulose, polyacrylamide and an additive to obtain an agglomeration agent, and mixing the agglomeration agent and water to obtain the agglomeration liquid; (2) agglomerating fine particles, namely spraying the agglomeration liquid into flue gas to cause fine particles in the sintering flue gas to be agglomerated to grow larger under the action of the agglomeration liquid; and (3) trapping by a dust removing device, namely trapping and removing the fine particles agglomerated to grow larger by the dust removing device. The method disclosed by the invention has the advantages that agglomeration liquid droplets adsorbing the fine particles are nucleated and collide with each other and grow to form large-particle agglomerates under the condition of low pressure, and a dust-removing device is adopted to remove the fine particles agglomerated to be larger, so that an all-new emission-reducing path is provided for reducing the emission of fine particles in the process of iron-ore sintering.
Description
Technical field
The present invention relates to Ore Sintering Process pollution reduction technical field, more particularly, it relates to a kind of method that agglomeration process suppresses the discharge of Ore Sintering Process fine particle.
Background technology
Pellet refers to the general name of the particulate matter that can pass through nose and mouth entrance human respiratory tract, represents (the surrounding air air kinetic diameter granule less than 10 microns) with PM10.PM2.5 refers to the surrounding air air kinetics equivalent diameter particulate matter less than or equal to 2.5 microns.It can be suspended in air the long period, and content concn is more high in atmosphere for it, just represents air pollution more serious.Although PM2.5 is the component that in earth atmosphere composition, content is little, but air quality and visibility etc. are had important impact by it.Compared with thicker Atmospheric particulates, PM2.5 particle diameter is little, area is big, and activity is strong, easily attaches poisonous and harmful substances (such as, heavy metal, microorganism etc.), and time of staying length in an atmosphere, fed distance are remote, thus the impact of health and atmosphere quality is bigger, and, it can enter human body alveolar even blood circulation, directly results in the diseases such as cardiovascular diseases.Current pellet pollutes oneself through becoming prominent atmospheric environment problem, causes the great attention of countries in the world.Health is had serious harm by it, is also the key factor causing the great environmental problem such as atmospheric visibility reduction, acid deposition, Global climate change, photochemical fog.Successively equal centering PM2.5 such as the air quality standard of the U.S., European Union, Britain etc. has clearly required；In February, 2012, new " ambient air quality " (GB3095-2012) of Environment Protect in China cloth promulgated by the ministries or commissions of the Central Government, it is additionally arranged PM2.5 mean concentration limit value.
Steel and iron industry is key pillars of the national economy industries, is again power consumption and heavy polluter.The crude steel annual production of current China alreadys more than 800,000,000 tons, close to the 50% of whole world yield.According to " Chinese environmental statistics annual report in 2012 ", ferrous metal smelting and rolling processing industry cigarette (powder) dirt discharge capacity is 181.3 ten thousand t, accounts for the 18.9% of major investigation industrial undertaking discharge capacity, is positioned at the 3rd.The source resolution of PM10 (particulate matters of particle diameter≤10 μm) and PM2.5 (particulate matters of particle diameter≤2.5 μm) shows, ferrous metallurgical industry has become as one of main source of PM10 and PM2.5 in China's air.Sintering circuit is requisite link in Production Processes In Steel Industry, but is maximum PM10 and the PM2.5 emission source of steel and iron industry, accounts for about the 40% of its total release[1-3].Due to agglomeration for iron mine be convulsion process and smoke moisture big, current sintering plant mainly adopts the particulate matter that electric cleaner comes in purifying sintering flue gas silently, electric cleaner is better to the coarseparticulate removal effect in flue gas silently, but for the particle diameter fine particle less than 10 μm, owing to it is higher than resistance, charge capacity is poor, efficiency of dust collection significantly reduces.Sintering flue gas is after electrostatic precipitation, and in flue gas, the particulate matter of more than 90% is PM10, and the particulate matter of more than 80% is PM2.5[4]。
Sintering flue gas is that the physicochemical change through series of complex is formed through sinter bed at down draft sintering process air.Owing to being subject to the impact of the factors such as material condition, mix material proportioning, technological parameter so that the complex chemical composition of sintering flue gas is changeable, flue gas flow, temperature and the fluctuation of each pollutant levels are very big.Being summed up, sintering flue gas has following typical feature[5-7]:
(1) sintering process air leak rate of air curtain is up to 40-50% so that produce exhaust gas volumn very big, produces 1t sintering deposit according to statistics and can produce 4000-6000m3Exhaust gas volumn；And exhaust gas volumn changes according to the difference of material composition, technological parameter so that exhaust gas volumn fluctuation is bigger；
(2) flue-gas temperature fluctuation range is big, changes with process conditions, fuel ratio, and flue-gas temperature exists: 80-160 DEG C of fluctuation；
(3) humidity of flue gas is relatively big, and moisture is about 10%.Sintered mix process needs add appropriate moisture carry out mixing, granulating, thus ensureing the breathability of the bed of material；
(4) big containing Dust Capacity in flue gas, wherein comprise a large amount of fine particle, sintering deposit per ton produces the dust of 20-40kg；
(5) smoke components is complicated, and it comprises multiple pollutant, as: fine particle, SO2, COx, NOx, HCl, HF and twos' English class etc..
The feature such as complicated just because of sintering smoke components, flow is big and pollutant levels are low, although sintering flue gas takes the cleaner of higher purification efficiency, but the removal effect of fine particle is unsatisfactory.
In sintering flue gas, fine particle is owing to specific surface area is big, surface activity strong, can be enriched with the poisonous and harmful substances such as the alkali metal (K, Na) of sintering process generation, heavy metal (Hg, Pb, Cr, Cu, Cd, As) and organic pollutant (VOCs, PCDD/Fs)[8], there is carcinogenic, mutagenesis and teratogenesis by force, be discharged into the aerosol that air is formed, be the key factor bringing out haze, acid rain, depletion of the ozone layer etc., its pollution problem is directly connected to living environment and the life quality of its people.The fine particle realizing sintering process reduces discharging extremely urgent.
Through retrieval, the existing emission-reduction technology scheme about flue gas fine particulate matter.As: the title of innovation and creation: industrial furnace smoke PM2.5Dust and heavy metal administer removal device[9], (China Patent No.: ZL201220721358.X, the applying date: 2012-12-24), by arranging filter bag, and by bag cage inside filter bag, to flue gas PM on flue gas path2.5Dust reduces discharging；Oarse-grained pollutant are had preferably with regard to emission reduction effect by this technology, but the PM in flue gas2.5Emission reduction effect limited.Additionally, the name of innovation and creation is called: a kind of method of agglomeration for iron mine flue gas stages cycle[10]A kind of method of (China Patent No.: ZL201310443223.0, the applying date: 2013-09-26), agglomeration for iron mine energy-saving and emission-reduction[11](China Patent No.: ZL201510137762.0, the applying date: 2015-03-27) etc., these technical schemes can realize the collaborative reduction of discharging of the multiple pollutant in sintering flue gas, although can reduce the discharge of big dust particle in flue gas；But the emission reduction effect of the fine particle in sintering flue gas is extremely limited.Sintering Gas phase Smoke is than other waste gas in addition, has the characteristics such as complicated component, flue gas flow are huge so that be applicable to sinter effective emission-reduction technology of flue gas fine particulate matter also untapped out.Exigence seeks the reduction of discharging approach being suitable for, it is achieved the reduction of discharging of the subparticle of sintering process.
List of references:
[1] Lv Yan. brief talk China's steel industry pollution situation and prophylactico-therapeutic measures [C] .2014 Jing-jin-ji region steel industry cleaning production environment protection exchanging meeting .2014,95-96.
[2] Yan Xianghong. Baoshan District of Shanghai air fine grained aerosol PM2.5 properties study and source resolution [D]. Shanghai: East China University of Science, 2011,42-50.
[3]S.JAGATHLAL.AssessingthePM10footprintofanironandsteelplantonambientairquality:ModellingPM10emissionsfromtheArcelormittalVanderbijlparkworksironandsteelplant[D].UniversityoftheWitwatersrand,Johanesburg,2012,1-5.
[4] horse capital. the granular material discharged characteristic research of iron and steel enterprise's typical production process [D]. Southwest University, 2009,24-28.
[5] Shen Xiaolin, Liu Daoqing, Lin Yu, etc. the research and development of Baosteel Sitnering Plant flue gas desulfurization technique and application [J]. bao steel technology, 2009 (3): 7-11.
[6]FuzhongW,WenhaoW.StudyonFlueGasDesulfurizationofSinteringinPilot-ScaleExperiment[C]//ComputerDistributedControlandIntelligentEnvironmentalMonitoring(CDCIEM),2011InternationalConferenceon.IEEE,2011:1737-1741.
[7] Chen Kaihua, Song Cunyi, Zhang Donghui, etc. the comparison [J] of sintering flue gas combined desulfurization and denitration technique. agglomerates of sintered pellets, 2008,33 (5): 29-32.
[8]C.PENG,Z.C.GUO,F.L.ZHANG.Discoveryofpotassiumchlorideinthesinteringdustbychemicalandphysicalcharacterization[J].ISIJInternational,2009,48(10):1398-1403.
[9] Liaoning ten thousand and environmental protection industry company limited. industrial furnace smoke PM2.5 dust and heavy metal administer removal device: China, ZL201220721358.X [P] .2013-09-11.
[10] Central South University. a kind of method of agglomeration for iron mine flue gas stages cycle: China, ZL201310443223.0 [P] .2014-01-08.
[11] Iron and Steel Research Geueral Inst, steel grinds bright Chinese workers journey Technology Co., Ltd.. a kind of method of agglomeration for iron mine energy-saving and emission-reduction: China, ZL201510137762.0 [P] .2015-07-01.
Summary of the invention
1. invention to solve the technical problem that
It is an object of the invention to overcome in prior art, Ore Sintering Process is the primary discharge source of fine particle, existing discharge-reducing method is difficult to the deficiency of the fine particle in sintering flue gas, a kind of method that offer and agglomeration process suppress the discharge of Ore Sintering Process fine particle, it is achieved effective elimination of sintering process fine particle.
2. technical scheme
For reaching above-mentioned purpose, technical scheme provided by the invention is:
A kind of agglomeration process of the present invention suppresses the method for Ore Sintering Process fine particle discharge, and concrete step is:
Step one: preparation reunion liquid, by sodium carboxymethyl cellulose, polyacrylamide and additive mix homogeneously, prepares agglomerator, agglomerator and water is mixed with and obtains reunion liquid；
Step 2: subparticle is reunited, and sprays in flue gas by reunion liquid, the fine particle in sintering flue gas is reunited under the effect of reunion liquid and is grown up；
Step 3: dust arrester traps, dust arrester trapping removes the fine particle grown up of reuniting.
Further, agglomerator includes aluminium polychlorid, sodium carboxymethyl cellulose, polyacrylamide and additive.
Further, each component of agglomerator forms according to following mass parts:
Further, step one: concretely comprising the following steps of preparation reunion liquid:
(A) weigh aluminium polychlorid 0-20 part, sodium carboxymethyl cellulose 20-40 part, polyacrylamide 20-40 part by mass parts, by aluminium polychlorid 0-20 part, sodium carboxymethyl cellulose 20-40 part, polyacrylamide 20-40 part mix homogeneously, obtain mixture A；
(B) weigh additive 2-5 part by mass parts, add in mixture A, mix homogeneously, obtain compound agglomerator；
(C) the compound agglomerator in step (B) is mixed with water, and be uniformly mixed, and the mass ratio of agglomerator and water is 1:2000-10000, prepares reunion liquid.
Further, reunion liquid adds Ca (OH)2Powder, the pH value regulating reunion liquid is 8-9.
Further, described additive is made up of activated carbon and coke powder, and additive is by following mass percent composition: activated carbon 70-90%, coke powder 10-30%.
Further, described activated carbon particle size requires: 74 μm≤activated carbon particle size≤100 μm, coke powder Particle size requirements: 74 μm≤coke powder particle diameter≤100 μm.
Further, step 2: what subparticle was reunited concretely comprises the following steps:
Described exhaust gases passes is the flue collector 1 of sintering flue gas, flue collector 1 is provided with atomization agglomeration device 2, spraying into vaporific reunion liquid mist and drip in atomization agglomeration device 2, the fine particle in flue gas and reunion liquid are grown up in reunite nucleation, the collision of atomization agglomeration device 2.
Further, the mist droplet particle size of the reunion liquid sprayed into is 30-150 μm, and the straying quatity of liquid of reuniting in every cubic metre of sintering flue gas is 10-20ml.
Further, atomization agglomeration device 2 includes collapsible tube 21, Cylindrical connecting tube 22 and expansion pipe 23.
3. beneficial effect
Adopt technical scheme provided by the invention, compared with existing known technology, there is following remarkable result:
A small amount of additive is added in proposing of the invention in agglomerator, significantly improve the reunion efficiency of reunion liquid, thus eliminating fine particle to adhere to the process of forming core, accelerate the reunion speed of particulate matter, and fine particle at a high speed is difficult to penetrate reunion liquid mist and drips, improve effective collision probability.
Owing to fine particle is had adsorption by the solid additive such as activated carbon and coke, after fine particle and reunion liquid mist drip collision entrance reunion liquid, can be attracted on activated carbon and coke, the liquid level that reunion liquid mist drips top layer is come out, new particulate matter can be fully contacted with reunion liquid mist dropping liquid face, thus improve reunion efficiency.With the addition of a small amount of additive, allow for PM10 and PM2.5 emission reduction efficiency and significantly improve, PM10 emission reduction efficiency has reached 65.9%, and PM2.5 emission reduction efficiency has reached 53.6%, achieves significant emission reduction effect.And, while reducing discharging fine particle, SO in sintering flue gas2、NOXConcentration of emission be significantly reduced, it is achieved that the Collaborative Control of multiple pollutant.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of embodiment 1-9；
Fig. 2 is the arrangement schematic diagram of the reunion liquid shower nozzle of the collapsible tube of embodiment 1-9；
Fig. 3 is sintering machine and the emission-reducing system schematic diagram of embodiment 1-9；
Fig. 4 is the reunion liquid shower nozzle position relationship schematic diagram with collapsible tube tube wall of embodiment 1-9；
Fig. 5 is the overall structure schematic diagram of embodiment 10；
Fig. 6 is the arrangement schematic diagram of the reunion liquid shower nozzle of the expansion pipe of embodiment 10；
Fig. 7 is the overall structure schematic diagram of embodiment 11；
Fig. 8 is that the expansion pipe of embodiment 11 arranges two and forms a team poly-liquid shower nozzle；
Fig. 9 is that embodiment 12 is reunited the structural representation that liquid shower nozzle is arranged in collapsible tube；
Figure 10 is the flow chart of fine particle discharge-reducing method of the present invention；
Figure 11 is that the present invention reunites the flow chart of liquid and preparation method thereof.
Label declaration in schematic diagram:
1, flue collector；2, atomization agglomeration device；21, collapsible tube；22, Cylindrical connecting tube；23, expansion pipe；3, reunion liquid adding apparatus；31, reunion liquid reservoir part；32, air compressor machine；33, reunion liquid shower nozzle；4, dust arrester；5, blower fan；6, pallet；7, bellows；8, circulating line；9, agitating device.
Detailed description of the invention
For further appreciating that present disclosure, below in conjunction with embodiment, the invention will be further described.
Embodiment 1
In conjunction with shown in Figure 10 and Figure 11, the present embodiment sinters a kind of method that agglomeration process suppresses the discharge of Ore Sintering Process fine particle: concrete reduction of discharging step is:
Step one: preparation reunion liquid
(A) weigh aluminium polychlorid 10g, sodium carboxymethyl cellulose 30g, polyacrylamide 30g by mass parts, by solid particle aluminium polychlorid 10g, sodium carboxymethyl cellulose 30g, polyacrylamide 30g mix homogeneously, obtain mixture A；
(B) weighing additive 2g by mass parts, described additive is solid additive, adds in mixture A, and mix homogeneously obtains compound agglomerator；
(C) the compound agglomerator in step (B) is mixed with water, and be uniformly mixed, and the mass ratio of agglomerator and water is 1:5000, then adds Ca (OH)2It is 8.5 that powder regulates solution PH, prepares reunion liquid；
Step 2: subparticle is reunited
In Ore Sintering Process, reunion liquid is added in reunion liquid reservoir part 31, flue collector 1 is provided with atomization agglomeration device 2, reunion liquid in reunion liquid reservoir part 31 is transported to reunion liquid shower nozzle 33 through air compressor machine 32, reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2, and the particulate matter in flue gas contacts in atomization agglomeration device 2 reunion with reunion liquid, moistening, adhesion, nucleation, collide, grow up.Wherein: the mist droplet particle size of the reunion liquid sprayed into is 30-150 μm, every cubic metre of straying quatity sintering liquid of reuniting in flue gas is 15ml.
nullAtomization agglomeration device 2 includes collapsible tube 21、Cylindrical connecting tube 22 and expansion pipe 23，Flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end，Expansion pipe 23 is flowed into again by Cylindrical connecting tube 22，Flue gas in flue collector 1 is flowed into collapsible tube 21 by collapsible tube 21 arrival end，Owing to collapsible tube 21 caliber diminishes rapidly，Flue gas flow rate in collapsible tube 21 is increased rapidly，Reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2，Make reunion liquid and the subparticle in flue gas and contact、Moistening、Adhere to，Owing to flue gas is increased by Cylindrical connecting tube 22 hourly velocity，Low pressure is produced at Cylindrical connecting tube 22 and expansion pipe 23，The reunion liquid mist being adsorbed with fine particle is made to drop in nucleation under low voltage situations、Collision、Grow up，The bulky grain aggregate formed.
Step 3: dust arrester traps
Adopt electrostatic precipitator by reunite grow up formed bulky grain aggregate remove, namely the highfield in electrostatic precipitator is utilized to make gas ionization, namely corona discharge is produced, and then make particle cluster separate from gas, thus suppressing the discharge of fine particle, it is achieved the reduction of discharging of subparticle in flue gas.
In Ore Sintering Process, spraying into reunion liquid in the exhaust gases passes of sintering flue gas, the fine particle in sintering flue gas is reunited under the effect of reunion liquid and is grown up, and adopts dust arrester 4 to remove the fine particle grown up of reuniting.
Flue gas fine particulate matter reduces discharging compound agglomerator, and each component forms according to following quality: aluminium polychlorid 10g, sodium carboxymethyl cellulose 30g, polyacrylamide 30g, additive 2g.Its additive is solid additive, described additive is made up of activated carbon and coke powder, described additive is by following mass percent composition: activated carbon 90%, coke powder 10%, described activated carbon particle size requires: 74 μm≤activated carbon particle size≤100 μm, coke powder Particle size requirements: 74 μm≤coke powder particle diameter≤100 μm.
Described exhaust gases passes is the flue collector 1 of sintering flue gas, flue collector 1 is provided with atomization agglomeration device 2, spraying into vaporific reunion liquid mist and drip in atomization agglomeration device 2, the fine particle in flue gas and reunion liquid are grown up in reunite nucleation, the collision of atomization agglomeration device 2.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, record is such as table 1.SO in sintering flue gas after detection dust arrester 42、NOXConcentration of emission, record such as table 2.
Comparative example 1
This comparative example is as reference test, the basic process of this comparative example, with embodiment 1, is different in that: be fitted without atomization agglomeration device 2 on flue collector, also without spraying into reunion liquid in flue collector 1, the concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, record is such as table 1.SO in sintering flue gas after detection dust arrester 42、NOXConcentration of emission, record such as table 2.
Comparative example 2
The reduction of discharging process of this comparative example is with embodiment 1, it is different in that: flue collector is fitted without atomization agglomeration device 2, but in flue collector 1, spray into reunion liquid, agglomerator is only made up of aluminium polychlorid, sodium carboxymethyl cellulose and polyacrylamide, without solid additive in agglomerator, the concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, record is such as table 1.
Comparative example 3
The reduction of discharging process of this comparative example is with embodiment 1, aluminium polychlorid, sodium carboxymethyl cellulose are identical with embodiment 1 with the weight/mass percentage composition of polyacrylamide, it is different in that: agglomerator is only made up of aluminium polychlorid, sodium carboxymethyl cellulose and polyacrylamide, without solid additive in agglomerator, the concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, record is such as table 1.
Test with the agglomerating effect of reunion efficiency rating PM10 (PM2.5), be defined as in flue gas PM10 (PM2.5) percentage ratio that its concentration reduces after reuniting, it may be assumed that
η=(1-N1/N0) × 100%
Wherein N0 is PM10 (PM2.5) concentration (mg/m in initial flue gas3), N1 is PM10 (PM2.5) concentration (mg/m in flue gas after reuniting3)。
PM10, PM2.5 concentration of emission in the flue gas of table 1 sintering test
| PM10(mg/m3) | PM10 emission reduction efficiency (%) | PM2.5(mg/m3) | PM2.5 emission reduction efficiency (%) | |
| Comparative example 1 | 12.6 | —— | 6.9 | —— |
| Comparative example 2 | 9.2 | 27.0% | 5.8 | 15.9% |
| Comparative example 3 | 6.9 | 45.2% | 4.8 | 30.4% |
| Embodiment 1 | 4.3 | 65.9% | 3.2 | 53.6% |
(1) contrasted by comparative example 1, comparative example 2, comparative example 3 and embodiment 1 it can be seen that liquid of no matter reuniting joins in flue gas in which way, the discharge of fine particle in flue gas can be reduced.
(2) comparative example 2 compares comparative example 1, PM10 emission reduction efficiency is 27.0%, PM2.5 emission reduction efficiency is 15.9%, and the emission reduction efficiency of fine particle is poor, and its reason is in that sintering process flue gas flow is big, general mode is adopted to add reunion liquid, make reunion liquid be difficult to be fully contacted with the particulate matter in flue gas, moistening, it is also difficult to the forming core realizing particulate matter is grown up, and sintering smoke components is complicated in addition, flue gas flow and composition fluctuation are big so that the emission reduction effect of fine particle is very limited.
(3) the PM10 emission reduction efficiency of comparative example 3 is 45.2%, and PM2.5 emission reduction efficiency is 30.4%, compares comparative example 2, and PM10 and PM2.5 emission reduction efficiency is significantly increased, and atomization agglomeration device 2 improves the reunion efficiency of reunion liquid significantly.Its reason of Analysis on Mechanism is in that: atomization agglomeration device 2 includes collapsible tube 21, Cylindrical connecting tube 22 and expansion pipe 23, flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end, owing to collapsible tube 21 caliber diminishes rapidly, flue gas flow rate in collapsible tube 21 is increased rapidly, reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2, make reunion liquid and the subparticle in flue gas and contact, moistening, adhere to, owing to flue gas is increased by Cylindrical connecting tube 22 hourly velocity, low pressure is produced at Cylindrical connecting tube 22 and expansion pipe 23, the reunion liquid mist being adsorbed with fine particle is made to drop in nucleation under low voltage situations, collision, grow up, the bulky grain aggregate formed.Adopt electrostatic precipitator by reunite grow up formed bulky grain aggregate remove so that in flue gas, the concentration of emission of fine particle significantly reduces.
What need to clearly state is herein, existing research worker generally believes that Venturi tube is poor to the emission reduction effect of fine particle, and owing to the drag losses of Venturi tube is bigger, the research that Venturi tube is applied to sintering flue gas fine particulate matter reduction of discharging is made to rarely have report, the applicant adopts Venturi effect to devise atomization agglomeration device 2 so that in flue gas, the concentration of emission of fine particle significantly reduces.Break the technology prejudice of prior art.
(4) comparative example 3 is compared, the PM10 emission reduction efficiency of embodiment 1 has reached 65.9%, PM2.5 emission reduction efficiency is 53.6%, solid additive in agglomerator significantly improves the reunion efficiency of reunion liquid, adopt electrostatic precipitator by reunite grow up formed bulky grain aggregate remove, the concentration of emission of fine particle in flue gas is significantly reduced, and this makes applicant very surprised；But its kinetic collision, adhesive mechanism are still not clear.By seminar for several times, its reaction mechanism is discussed, and thinks that its reason is probably:
1) flue gas is increased by Cylindrical connecting tube 22 hourly velocity, form lower pressure environment, reunion liquid is made to collide with fine particle, grow up under low voltage situations, when reunion liquid mist includes solid additive in dripping, solid additive is dripped in reunion liquid mist and is internally formed a stable forming core parent, after fine particle contacts with reunion liquid droplet surface, the bulky grain aggregate directly formed, eliminate fine particle and adhere to the process of forming core, thus accelerating the reunion speed of particulate matter.
2) fine particle is reunited and is mainly relied on reunion liquid mist to drip to contact with fine particle, collide and grow up, but the flue gas flow rate in collapsible tube 21 increases rapidly, although improve reunion liquid mist to drip and the probability of fine particle collision, but the speed dripped due to fine particle and reunion liquid mist in flue gas is bigger, in the process of contact-impact, have part fine particle to be directed through reunion liquid mist to drip so that reunion liquid is difficult to absorption fine particle, forms a large amount of invalid collision；When reunion liquid mist includes solid additive in dripping, fine particle at a high speed is difficult to penetrate reunion liquid mist and drips, and improves effective collision probability.
3) after fine particle and reunion liquid mist drip collision entrance reunion liquid, the impact of the viscous resistance owing to being subject to during reunion liquid mist is dripped, fine particle can again rest on reunion liquid mist and drip top layer, without dripping inside in reunion liquid mist；And liquid mist of reuniting is dripped and sticking of particulate matter is relied primarily on the surface layer that reunion liquid mist is dripped, dripping top layer when poly-liquid mist and be constantly occupied full, new particulate matter and reunion liquid mist can not be sticked owing to not reaching the liquid level of droplet when dripping collision；When reunion liquid mist includes solid additive in dripping, owing to solid additive has loose structure, fine particle there is adsorption, after fine particle and reunion liquid mist drip collision entrance reunion liquid, can be attracted on activated carbon and coke, the liquid level that reunion liquid mist drips top layer is come out, and new particulate matter can be fully contacted with reunion liquid mist dropping liquid face, thus improve reunion efficiency.
nullThe atomization agglomeration device 2 of the present invention includes collapsible tube 21、Cylindrical connecting tube 22 and expansion pipe 23，Flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end，Expansion pipe 23 is flowed into again by Cylindrical connecting tube 22，Flue gas in flue collector 1 is flowed into collapsible tube 21 by collapsible tube 21 arrival end，Owing to collapsible tube 21 caliber diminishes rapidly，Flue gas flow rate in collapsible tube 21 is increased rapidly，Reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2，Make reunion liquid and the subparticle in flue gas and contact、Moistening、Adhere to，Owing to flue gas is increased by Cylindrical connecting tube 22 hourly velocity，Low pressure is produced at Cylindrical connecting tube 22 and expansion pipe 23，The reunion liquid mist being adsorbed with fine particle is made to drop in nucleation under low voltage situations、Collision、Grow up，The bulky grain aggregate formed.And adopting dust arrester to remove the fine particle grown up of reuniting, it is achieved that the efficient emission-reducing of fine particle, the reduction of discharging for Ore Sintering Process fine particle provides brand-new reduction of discharging approach.
A small amount of additive is added in proposing of the invention in agglomerator, significantly improve the reunion efficiency of reunion liquid, thus eliminating fine particle to adhere to the process of forming core, accelerate the reunion speed of particulate matter, and fine particle at a high speed is difficult to penetrate reunion liquid mist and drips, improve effective collision probability.
Owing to activated carbon and coke have loose structure, fine particle there is adsorption, after fine particle and reunion liquid mist drip collision entrance reunion liquid, can be attracted on activated carbon and coke, the liquid level that reunion liquid mist drips top layer is come out, new particulate matter can be fully contacted with reunion liquid mist dropping liquid face, thus improve reunion efficiency.With the addition of a small amount of additive, allow for PM10 and PM2.5 emission reduction efficiency and significantly improve, PM10 emission reduction efficiency has reached 65.9%, and PM2.5 emission reduction efficiency has reached 53.6%, achieves significant emission reduction effect.
SO2、NOXEmission reduction efficiency adopt below equation be calculated:
Wherein C0 is PM10 (PM2.5) concentration (mg/m in initial flue gas3), C1 is PM10 (PM2.5) concentration (mg/m in flue gas after reuniting3)。
SO in the flue gas of table 2 sintering test2、NOXConcentration of emission
| SO2(mg/m3) | SO2Emission reduction efficiency (%) | NOX(mg/m3) | NOXEmission reduction efficiency (%) | |
| Comparative example 1 | 659 | —— | 322 | —— |
| Embodiment 1 | 378 | 42.6% | 256 | 20.5% |
As shown in Table 2, the SO after spraying into the agglomerator of the present invention, in flue gas2Concentration of emission by 659mg/m3Drop to 378mg/m3, NOXConcentration of emission by 322mg/m3Drop to 256mg/m3, not only fine particle is had adsorption, also to the SO in flue gas2, NOx, two English have adsorption, thus realizing the Collaborative Control of multiple pollutant.Its reason is in that: include activated carbon in the agglomerator solution sprayed into and coke has loose structure, not only fine particle is had adsorption, also to the SO in flue gas2, NOx, two English have adsorption, and add Ca (OH) in reunion liquid2Powder, it is possible to the SO in absorption flue gas2, the sour gas such as NOx；And promote fine particle drip with reunion liquid mist contact, moistening, adhesion, thus improving reunion efficiency.
In conjunction with Fig. 1, 2, shown in 3 and 4, this method application emission-reducing system, it is atomized agglomeration device 2 including fine particle, reunion liquid adding apparatus 3 and dust arrester 4, sinter mixture is blended, by distribution device after granulation, dress is layered on sintering pallet 6, sinter mixture carries out down draft sintering after igniting, sintering flue gas traverse sinter bed, it is connected with flue collector 1 by bellows 7 bottom pallet 6, convulsion flue gas is imported in flue collector 1 by bottom pallet 6 through bellows 7, flue collector 1 arranges atomization agglomeration device 2, reunion liquid adding apparatus 3 and dust arrester 4, flue gas is flowed into atomization agglomeration device 2 by flue collector 1, chimney is entered by blower fan 5 after removing dust device 4 dedusting；Fine particle in flue gas is reunion forming core in atomization agglomeration device 2, nucleation and growth process, and removes the fine particle grown up of reuniting in the dust arrester 4 at rear portion.
Above-mentioned atomization agglomeration device 2 includes collapsible tube 21, Cylindrical connecting tube 22 and expansion pipe 23；Wherein: collapsible tube 21 is the different conical pipe of two ends internal diameter with expansion pipe 23, one end that described collapsible tube 21 is connected with flue collector 1 is collapsible tube 21 arrival end, the internal diameter of collapsible tube 21 arrival end is identical with the internal diameter of flue collector 1, collapsible tube 21 is collapsible tube 21 port of export near one end of expansion pipe 23, and collapsible tube 21 port of export is identical with expansion pipe 23 arrival end internal diameter；Collapsible tube 21 port of export is connected by Cylindrical connecting tube 22 with expansion pipe 23 arrival end, and described expansion pipe 23 is expansion pipe 23 port of export away from one end of collapsible tube 21, and expansion pipe 23 port of export internal diameter is identical with the internal diameter of flue collector 1, and is connected with flue collector 1；The centrage of above-mentioned collapsible tube 21, Cylindrical connecting tube 22 and expansion pipe 23 is on same straight line；Flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end, then is flowed into expansion pipe 23 by Cylindrical connecting tube 22, and is flowed out atomization agglomeration device 2 by expansion pipe 23 port of export.Flue gas in flue collector 1 is flowed into collapsible tube 21 by collapsible tube 21 arrival end, owing to collapsible tube 21 caliber diminishes rapidly, flue gas flow rate in collapsible tube 21 is increased rapidly, flue gas is increased by Cylindrical connecting tube 22 hourly velocity, produce low pressure in its vicinity so that the particulate matter collision in flue gas is more violent.
Described reunion liquid adding apparatus 3 includes reunion liquid reservoir part 31, air compressor machine 32 and reunion liquid shower nozzle 33, wherein reunion liquid reservoir part 31 is provided with agitating device 9, make the reunion liquid uniform component in reunion liquid reservoir part 31 stable, prevent the reunion liquid generation component segregation being made into, thus affecting the emission reduction effect of fine particle.Reunion liquid reservoir part 31 is connected with the entrance point of air compressor machine 32 by pipeline, air compressor machine 32 port of export is connected with reunion liquid shower nozzle 33 by pipeline, wherein: reunion liquid reservoir part 31 is used for storing reunion liquid, air compressor machine 32 enters reunion liquid shower nozzle 33 for reunion liquid and provides power, reunion liquid shower nozzle 33 is for by reunion liquid mist, and spraying into atomization agglomeration device 2, described reunion liquid shower nozzle 33 is arranged on collapsible tube 21.Reunion liquid containing agglomerator is under the driving of air compressor machine 32, and by flowing into reunion liquid shower nozzle 33 in reunion liquid reservoir part 31, atomization reunion liquid is sprayed into atomization agglomeration device 2 by reunion liquid shower nozzle 33, and the mist droplet particle size after atomization is 30-150 μm；Collapsible tube 21 caliber of atomization agglomeration device 2 diminishes rapidly, make flue gas pass through Cylindrical connecting tube 22 hourly velocity to increase, produce low pressure in its vicinity, so that subparticle is produced adsorption by reunion liquid, particulate matter in flue gas with atomization after reunion liquid be fully contacted, moistening, adhesion, nucleation, continuous reunion collision is grown up so that subparticle is constantly reunited and grown up.
Reunion liquid shower nozzle 33 is arranged on the tangent to periphery of collapsible tube 21 cross section uniformly, and the flue gas flow rate in collapsible tube 21 constantly increases, and the reunion liquid mist after the atomization of reunion liquid shower nozzle 33 is dripped can abundant with flue gas in collapsible tube 21, Homogeneous phase mixing；This cross section is the vertical tangent plane of the centrage being perpendicular to collapsible tube 21, the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is L1, the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 port of export is L2, L2=0.5L1, namely the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is more than the horizontal range of reunion liquid shower nozzle 33 place plane Yu collapsible tube 21 port of export, make flue gas after entering collapsible tube 21, the process that flue gas flow rate increases is dripped mixing with the reunion liquid mist after atomization, contacted.
Angle between reunion liquid shower nozzle 33 centrage and collapsible tube 21 tube wall is a, a=45 °, present and collapsible tube 21 tube walls parallel state at collapsible tube 21 edge airflow, when a=45 °, if the speed that the reunion liquid mist that reunion liquid shower nozzle 33 sprays into is dripped is v, then it is vcosa along the speed of collapsible tube 21 tube wall, increases reunion liquid mist and drips and the collision probability of granule in flue gas；Additionally, reunion liquid mist is dripped constantly to collapsible tube 21 central motion so that be also fully contacted with the flue gas of collapsible tube 21 center.Collapsible tube 21 cross section is provided with 16 reunion liquid shower nozzles 33 uniformly, promote reunion liquid mist drip contact with the fine particle in collapsible tube 21, moistening, adhesion.
The disposed outside of collapsible tube 21 has circulating line 8, circulating line 8 entrance point is connected with air compressor machine 32 port of export, being provided with 16 outlets on circulating line 8, and the outlet of circulating line 8 is connected with reunion liquid shower nozzle 33, reunion liquid is flowed into reunion liquid shower nozzle 33 by circulating line 8；Circulating line 8 is provided with 16 outlets, uniform and stable for liquid of reuniting can be transported to reunion liquid shower nozzle 33 from reunion liquid reservoir part 31 so that what reunion liquid shower nozzle 33 was uniform, stable sprays into reunion liquid.
Described dust arrester 4 is electrostatic precipitator, fine particle in flue gas drips moistening, adhesion at atomization agglomeration device 2 with reunion liquid mist, further forming core, grow up after, by electrostatic precipitator, the particulate matter after growing up is removed, the reunion that can realize sintering process fine particle reduces discharging.
Embodiment 2
The substance of the present embodiment is with embodiment 1, it is different in that: described additive is made up of activated carbon and zeolite, additive is by following mass percent composition: activated carbon 85%, zeolite 15%, described activated carbon particle size requires: 74 μm≤activated carbon particle size≤100 μm, and sized zeolite particles requires: 74 μm≤sized zeolite particles≤100 μm.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 56.4%, and the emission reduction efficiency of PM10 is 49.0%.
Embodiment 3
The substance of the present embodiment is with embodiment 1, and it is different in that: described additive is made up of activated carbon and zeolite, and additive is by following mass percent composition: activated carbon 95%, zeolite 5%.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 60.2%, and the emission reduction efficiency of PM10 is 48.8%.
Embodiment 4
The substance of the present embodiment is with embodiment 1, and it is different in that: described additive is made up of activated carbon and zeolite, and additive is by following mass percent composition: activated carbon 90%, zeolite 10%.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 55.9%, and the emission reduction efficiency of PM10 is 48.6%.
Embodiment 5
The substance of the present embodiment is with embodiment 1, it is different in that: described additive is become with Suzhou local soil type by activated carbon, coke powder, bentonite, described additive is by following mass percent composition: activated carbon 90%, coke powder 8%, bentonite 1%, Suzhou soil 1%, described bentonite Particle size requirements: 74 μm≤bentonite particle diameter≤100 μm, Suzhou soil Particle size requirements: grogs footpath≤100 μm, 74 μm≤Suzhou.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 63.8%, and the emission reduction efficiency of PM10 is 54.2%.
Embodiment 6
The substance of the present embodiment is with embodiment 1, it is different in that: described additive is made up of activated carbon, coke powder and Kaolin, described additive is by following mass percent composition: activated carbon 90%, coke powder 7%, Kaolin 3%, described Kaolin Particle size requirements: 74 μm≤Kaolin particle diameter≤100 μm.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 64.2%, and the emission reduction efficiency of PM10 is 51.1%.
Embodiment 7
The substance of the present embodiment is with embodiment 1, and it is different in that: described additive is made up of activated carbon, coke powder, Kaolin and zeolite, and described additive is by following mass percent composition: activated carbon 90%, coke powder 7%, Kaolin 2%, zeolite 1%.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 62.6%, and the emission reduction efficiency of PM10 is 51.7%.
Embodiment 8
The substance of the present embodiment is with embodiment 1, and it is different in that: agglomeration process suppresses the method for Ore Sintering Process fine particle discharge:
Step one: preparation reunion liquid
(A) weigh sodium carboxymethyl cellulose 20g, polyacrylamide 20g by mass parts, by solid particle sodium carboxymethyl cellulose 20g, polyacrylamide 20g mix homogeneously, obtain mixture A；
(B) weigh additive 4g by mass parts, add in mixture A, mix homogeneously, obtain compound agglomerator；
(C) the compound agglomerator in step (B) is mixed with water, and be uniformly mixed, and the mass ratio of agglomerator and water is 1:2000, then adds Ca (OH)2It is 8 that powder regulates solution PH, prepares reunion liquid；
Step 2: subparticle is reunited
In Ore Sintering Process, reunion liquid is added in reunion liquid reservoir part 31, flue collector 1 is provided with atomization agglomeration device 2, reunion liquid in reunion liquid reservoir part 31 is transported to reunion liquid shower nozzle 33 through air compressor machine 32, reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2, and the particulate matter in flue gas contacts in atomization agglomeration device 2 reunion with reunion liquid, moistening, adhesion, nucleation, collide, grow up.Wherein: the mist droplet particle size of the reunion liquid sprayed into is 30-150 μm, every cubic metre of straying quatity sintering liquid of reuniting in flue gas is 20ml.
nullAtomization agglomeration device 2 includes collapsible tube 21、Cylindrical connecting tube 22 and expansion pipe 23，Flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end，Expansion pipe 23 is flowed into again by Cylindrical connecting tube 22，Flue gas in flue collector 1 is flowed into collapsible tube 21 by collapsible tube 21 arrival end，Owing to collapsible tube 21 caliber diminishes rapidly，Flue gas flow rate in collapsible tube 21 is increased rapidly，Reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2，Make reunion liquid and the subparticle in flue gas and contact、Moistening、Adhere to，Owing to flue gas is increased by Cylindrical connecting tube 22 hourly velocity，Low pressure is produced at Cylindrical connecting tube 22 and expansion pipe 23，The reunion liquid mist being adsorbed with fine particle is made to drop in nucleation under low voltage situations、Collision、Grow up，The bulky grain aggregate formed.
Step 3: dust arrester traps
Adopt sack cleaner by reunite grow up formed bulky grain aggregate remove, namely utilize sack cleaner, and then make particle cluster separate from gas, it is achieved the reduction of discharging of subparticle in flue gas.
Additive is by following mass percent composition: activated carbon 70%, coke powder 30%.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 60.7%, and the emission reduction efficiency of PM10 is 43.5%.
The horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is L1, the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 port of export is L2, L2=L1, namely the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is equal to the horizontal range of reunion liquid shower nozzle 33 place plane with collapsible tube 21 port of export, make flue gas after collapsible tube 21, the process that flue gas flow rate increases is dripped mixing with the reunion liquid mist after atomization, contacted.
Angle between reunion liquid shower nozzle 33 centrage and collapsible tube 21 tube wall is a, a=30 °, present and collapsible tube 21 tube walls parallel state at collapsible tube 21 edge airflow, when a=30 °, the speed that the reunion liquid mist that reunion liquid shower nozzle 33 sprays into is dripped is v, then it is vcosa along the speed of collapsible tube 21 tube wall, increases reunion liquid mist and drips and the collision probability of granule in flue gas；Additionally, reunion liquid mist is dripped constantly to collapsible tube 21 central motion so that be also fully contacted with the flue gas of collapsible tube 21 center.Collapsible tube 21 cross section is provided with 8 reunion liquid shower nozzles 33 uniformly, promote reunion liquid mist drip contact with the flue gas particle in collapsible tube 21, moistening, adhesion.
The disposed outside of collapsible tube 21 has circulating line 8, circulating line 8 entrance point is connected with air compressor machine 32 port of export, being provided with 8 outlets on circulating line 8, and the outlet of circulating line 8 is connected with reunion liquid shower nozzle 33, reunion liquid is flowed into reunion liquid shower nozzle 33 by circulating line 8；Circulating line 8 is provided with 8 outlets, uniform and stable for liquid of reuniting can be transported to reunion liquid shower nozzle 33 from reunion liquid reservoir part 31 so that what reunion liquid shower nozzle 33 was uniform, stable sprays into reunion liquid.
Embodiment 9
The substance of the present embodiment is with embodiment 1, and it is different in that: agglomeration process suppresses the method for Ore Sintering Process fine particle discharge:
Step one: preparation reunion liquid
(A) weigh aluminium polychlorid 20g, sodium carboxymethyl cellulose 40g, polyacrylamide 40g by mass parts, by solid particle aluminium polychlorid 20g, sodium carboxymethyl cellulose 40g, polyacrylamide 40g mix homogeneously, obtain mixture A；
(B) weigh additive 5g by mass parts, add in mixture A, mix homogeneously, obtain compound agglomerator；
(C) the compound agglomerator in step (B) is mixed with water, and be uniformly mixed, and the mass ratio of agglomerator and water is 1:10000, then adds Ca (OH)2It is 9 that powder regulates solution PH, prepares reunion liquid；
Step 2: subparticle is reunited
In Ore Sintering Process, reunion liquid is added in reunion liquid reservoir part 31, flue collector 1 is provided with atomization agglomeration device 2, reunion liquid in reunion liquid reservoir part 31 is transported to reunion liquid shower nozzle 33 through air compressor machine 32, reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in atomization agglomeration device 2 collapsible tube 21, and the particulate matter in flue gas contacts in atomization agglomeration device 2 reunion with reunion liquid, moistening, adhesion, nucleation, collide, grow up.Wherein: the mist droplet particle size of the reunion liquid sprayed into is 30-150 μm, every cubic metre of straying quatity sintering liquid of reuniting in flue gas is 10ml.
nullAtomization agglomeration device 2 includes collapsible tube 21、Cylindrical connecting tube 22 and expansion pipe 23，Flue gas is entered atomization agglomeration device 2 by collapsible tube 21 arrival end，Expansion pipe 23 is flowed into again by Cylindrical connecting tube 22，Flue gas in flue collector 1 is flowed into collapsible tube 21 by collapsible tube 21 arrival end，Owing to collapsible tube 21 caliber diminishes rapidly，Flue gas flow rate in collapsible tube 21 is increased rapidly，Reunion liquid shower nozzle 33 sprays into vaporific reunion liquid in the collapsible tube 21 of atomization agglomeration device 2，Make reunion liquid and the subparticle in flue gas and contact、Moistening、Adhere to，Owing to flue gas is increased by Cylindrical connecting tube 22 hourly velocity，Low pressure is produced at Cylindrical connecting tube 22 and expansion pipe 23，The reunion liquid mist being adsorbed with fine particle is made to drop in nucleation under low voltage situations、Collision、Grow up，The bulky grain aggregate formed.
Step 3: dust arrester traps
Adopt sack cleaner by reunite grow up formed bulky grain aggregate remove, namely utilize sack cleaner, and then make particle cluster separate from gas, it is achieved the reduction of discharging of subparticle in flue gas.
Additive is by following mass percent composition: activated carbon 85%, coke powder 15%.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 61.9%, and the emission reduction efficiency of PM10 is 52.6%.
The horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is L1, the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 port of export is L2, L2=0.8L1, namely the horizontal range of reunion liquid shower nozzle 33 place plane and collapsible tube 21 arrival end is more than the horizontal range of reunion liquid shower nozzle 33 place plane Yu collapsible tube 21 port of export, make flue gas after collapsible tube 21, the process that flue gas flow rate increases is dripped mixing with the reunion liquid mist after atomization, contacted.
Angle between reunion liquid shower nozzle 33 centrage and collapsible tube 21 tube wall is a, a=35 °, present and collapsible tube 21 tube walls parallel state at collapsible tube 21 edge airflow, when a=35 °, the speed that the reunion liquid mist that reunion liquid shower nozzle 33 sprays into is dripped is v, then it is vcosa along the speed of collapsible tube 21 tube wall, increases reunion liquid mist and drips and the collision probability of granule in flue gas；Additionally, reunion liquid mist is dripped constantly to collapsible tube 21 central motion so that be also fully contacted with the flue gas of collapsible tube 21 center.Collapsible tube 21 cross section is provided with 2 reunion liquid shower nozzles 33 uniformly, promote reunion liquid mist drip contact with the flue gas particle in collapsible tube 21, moistening, adhesion.
The disposed outside of collapsible tube 21 has circulating line 8, circulating line 8 entrance point is connected with air compressor machine 32 port of export, being provided with 2 outlets on circulating line 8, and the outlet of circulating line 8 is connected with reunion liquid shower nozzle 33, reunion liquid is flowed into reunion liquid shower nozzle 33 by circulating line 8；Circulating line 8 is provided with 2 outlets, can uniform and stable for liquid of reuniting is transported to reunion liquid shower nozzle 33 from reunion liquid reservoir part 31 so that reunion liquid shower nozzle 33 sprays into reunion liquid for uniform, stable.
Embodiment 10
The substance of the present embodiment is with embodiment 1, and it is different in that:
As shown in Figure 5 and Figure 6, collapsible tube 21 is provided with reunion liquid shower nozzle 33, and reunion liquid shower nozzle 33 is arranged on the tangent to periphery of collapsible tube 21 cross section uniformly.Expansion pipe 23 is also equipped with reunion liquid shower nozzle 33, and reunion liquid shower nozzle 33 is arranged on the tangent to periphery of expansion pipe 23 cross section uniformly.And collapsible tube 21 is connected with same reunion liquid reservoir part 31 with the reunion liquid shower nozzle 33 on expansion pipe 23, in collapsible tube 21, every cubic metre of straying quatity sintering liquid of reuniting in flue gas is 14ml, and the straying quatity of liquid of reuniting in every cubic metre of sintering flue gas in expansion pipe 23 is 1ml.
The disposed outside of expansion pipe 23 has circulating line 8, circulating line 8 entrance point is connected with air compressor machine 32 port of export, being provided with 16 outlets on circulating line 8, and the outlet of circulating line 8 is connected with reunion liquid shower nozzle 33, reunion liquid is flowed into reunion liquid shower nozzle 33 by circulating line 8；Circulating line 8 is provided with 16 outlets, uniform and stable for liquid of reuniting can be transported to reunion liquid shower nozzle 33 from reunion liquid reservoir part 31 so that what reunion liquid shower nozzle 33 was uniform, stable sprays into reunion liquid.
Above-mentioned reunion liquid shower nozzle 33 is connected with air compressor machine 32 also by pipeline, air compressor machine 32 is connected with reunion liquid reservoir part 31, wherein: reunion liquid reservoir part 31 is used for storing reunion liquid, air compressor machine 32 enters reunion liquid shower nozzle 33 for reunion liquid and provides power, reunion liquid shower nozzle 33 is used for reunion liquid mist, and sprays into atomization agglomeration device 2.Reunion liquid containing agglomerator is under the driving of air compressor machine 32, and by flowing into reunion liquid shower nozzle 33 in reunion liquid reservoir part 31, atomization reunion liquid is sprayed into atomization agglomeration device 2 by reunion liquid shower nozzle 33, and the mist droplet particle size after atomization is 30-150 μm.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 67.7%, and the emission reduction efficiency of PM10 is 54.5%.
Its reason is in that: be provided with reunion liquid shower nozzle 33 on collapsible tube 21 and expansion pipe 23.Fine particle in collapsible tube 21 is fully contacted with reunion liquid, is agglomerated liquid mist and drips moistening, adhesion, and forms reunion core；Expansion pipe 23 is also equipped with reunion liquid shower nozzle 33, and spraying into after reunion liquid mist drips, reunion liquid mist drips the reunion core moistening formed by fine particle again, when fine particle and reunion core crash, easily it is agglomerated core to adhere to, and grows up gradually in constantly collision.
Embodiment 11
The substance of the present embodiment is with embodiment 1, and it is different in that:
As it is shown in fig. 7, be provided with reunion liquid shower nozzle 33 on collapsible tube 21, and reunion liquid shower nozzle 33 is arranged on the tangent to periphery of collapsible tube 21 cross section uniformly.Expansion pipe 23 is also equipped with reunion liquid shower nozzle 33, and reunion liquid shower nozzle 33 is arranged on the tangent to periphery of expansion pipe 23 cross section uniformly.And collapsible tube 21 is respectively arranged with separate reunion liquid adding apparatus 3 with expanding on pipe 23.Namely reunion liquid shower nozzle on collapsible tube 21 33 forms a team poly-liquid reservoir part 31 and air compressor machine 32 is connected with one, and expand reunion liquid shower nozzle on pipe 23 33 and form a team poly-liquid reservoir part 31 with another and air compressor machine 32 is connected so that the collapsible tube 21 and reunion liquid of variable concentrations and kind can be sprayed in expansion pipe 23.The mass ratio of the agglomerator in the reunion liquid that wherein collapsible tube 21 sprays into and water is 1:5000, agglomerator and the mass ratio of water in the reunion liquid that expansion pipe 23 sprays into are 1:10000, in collapsible tube 21, every cubic metre of straying quatity sintering liquid of reuniting in flue gas is 14ml, and the straying quatity of liquid of reuniting in every cubic metre of sintering flue gas in expansion pipe 23 is 0.5ml.The disposed outside of expansion pipe 23 has circulating line 8, circulating line 8 entrance point is connected with air compressor machine 32 port of export, being provided with 16 outlets on circulating line 8, and the outlet of circulating line 8 is connected with reunion liquid shower nozzle 33, reunion liquid is flowed into reunion liquid shower nozzle 33 by circulating line 8；Circulating line 8 is provided with 16 outlets, uniform and stable for liquid of reuniting can be transported to reunion liquid shower nozzle 33 from reunion liquid reservoir part 31 so that what reunion liquid shower nozzle 33 was uniform, stable sprays into reunion liquid.
Above-mentioned reunion liquid shower nozzle 33 is connected with air compressor machine 32 also by pipeline, air compressor machine 32 is connected with reunion liquid reservoir part 31, wherein: reunion liquid reservoir part 31 is used for storing reunion liquid, air compressor machine 32 enters reunion liquid shower nozzle 33 for reunion liquid and provides power, reunion liquid shower nozzle 33 is used for reunion liquid mist, and sprays into atomization agglomeration device 2.Reunion liquid containing agglomerator is under the driving of air compressor machine 32, and by flowing into reunion liquid shower nozzle 33 in reunion liquid reservoir part 31, atomization reunion liquid is sprayed into atomization agglomeration device 2 by reunion liquid shower nozzle 33, and the mist droplet particle size after atomization is 30-150 μm.
The concentration of emission of PM2.5 and PM10 in sintering flue gas after detection dust arrester 4, and calculate the emission reduction efficiency of PM2.5 and PM10, the emission reduction efficiency of PM2.5 is 67.3%, and the emission reduction efficiency of PM10 is 54.2%.
Emission reduction efficiency is higher than embodiment 1, and its reason of Analysis on Mechanism is in that: be provided with reunion liquid shower nozzle 33 on collapsible tube 21 and expansion pipe 23.Fine particle in collapsible tube 21 is fully contacted with reunion liquid, is agglomerated liquid mist and drips moistening, adhesion, and forms reunion core；Expansion pipe 23 is also equipped with reunion liquid shower nozzle 33, and spraying into after reunion liquid mist drips, reunion liquid mist drips the reunion core moistening formed by fine particle again, when fine particle and reunion core crash, easily it is agglomerated core to adhere to, and grows up gradually in constantly collision.
In addition, as shown in Figure 8, expansion pipe 23 has on the tangent to periphery of two cross sections to be uniformly arranged reunion liquid shower nozzle 33, and namely expansion pipe 23 is provided with two and forms a team poly-liquid shower nozzle 33, thus realization classification in expansion pipe 23 sprays into reunion liquid mist and drips, improve the service efficiency of reunion liquid.Reason is in that: reunion liquid mist is dripped and sticking of particulate matter is relied primarily on the surface layer that reunion liquid mist is dripped, and drips top layer when poly-liquid mist and is constantly occupied full, and new particulate matter and reunion liquid mist can not be sticked owing to not reaching the liquid level of droplet when dripping collision；Reunion liquid classification adds fashionable, it is possible to reunion liquid is constantly combined with subparticle so that reunion liquid mist is dripped and is constantly exposed to granule top layer, and new particulate matter can be fully contacted with reunion liquid mist dropping liquid face, thus improve reunion efficiency.
Embodiment 12
The substance of the present embodiment is with embodiment 1, and it is different in that:
As shown in Figure 9, described reunion liquid shower nozzle 33 is arranged in collapsible tube 21 manages, reunion liquid shower nozzle 33 is contrary with the airflow direction in flue collector 1, i.e. reunion liquid mist is dripped and is sprayed into collapsible tube 21 central part by reunion liquid shower nozzle 33, and the droplet direction of reunion liquid shower nozzle 33 ejection is contrary with airflow direction in flue collector 1, increases reunion liquid mist and drips and the collision probability of granule in flue gas；Additionally, reunion liquid mist is dripped constantly to collapsible tube 21 central motion so that be also fully contacted with the flue gas of collapsible tube 21 center.
Schematically the present invention and embodiment thereof being described above, this description does not have restricted, and shown in accompanying drawing is also one of embodiments of the present invention, and actual structure is not limited thereto.So, if those of ordinary skill in the art is enlightened by it, when without departing from the invention objective, design the frame mode similar to this technical scheme and embodiment without creationary, protection scope of the present invention all should be belonged to.
Claims (10)
1. the method that an agglomeration process suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: concrete step is:
Step one: preparation reunion liquid, by sodium carboxymethyl cellulose, polyacrylamide and additive mix homogeneously, prepares agglomerator, agglomerator and water is mixed with and obtains reunion liquid；
Step 2: subparticle is reunited, and sprays in flue gas by reunion liquid, the fine particle in sintering flue gas is reunited under the effect of reunion liquid and is grown up；
Step 3: dust arrester traps, dust arrester (4) trapping removes the fine particle grown up of reuniting.
2. the method that a kind of agglomeration process according to claim 1 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: agglomerator includes aluminium polychlorid, sodium carboxymethyl cellulose, polyacrylamide and additive.
3. the method that a kind of agglomeration process according to claim 2 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: each component of agglomerator forms according to following mass parts:
4. the method that a kind of agglomeration process according to claim 3 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: step one: concretely comprising the following steps of preparation reunion liquid:
(A) weigh aluminium polychlorid 0-20 part, sodium carboxymethyl cellulose 20-40 part, polyacrylamide 20-40 part by mass parts, by aluminium polychlorid 0-20 part, sodium carboxymethyl cellulose 20-40 part, polyacrylamide 20-40 part mix homogeneously, obtain mixture A；
(B) weigh additive 2-5 part by mass parts, add in mixture A, mix homogeneously, obtain compound agglomerator；
(C) the compound agglomerator in step (B) is mixed with water, and be uniformly mixed, and the mass ratio of agglomerator and water is 1:2000-10000, prepares reunion liquid.
5. the method that a kind of agglomeration process according to claim 4 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: in reunion liquid, add Ca (OH)2Powder, the pH value regulating reunion liquid is 8-9.
6. the method that a kind of agglomeration process according to claim 5 suppresses the discharge of Ore Sintering Process fine particle, it is characterized in that: described additive is made up of activated carbon and coke powder, additive is by following mass percent composition: activated carbon 70-90%, coke powder 10-30%.
7. the method that a kind of agglomeration process according to claim 6 suppresses the discharge of Ore Sintering Process fine particle, it is characterized in that: described activated carbon particle size requires: 74 μm≤activated carbon particle size≤100 μm, coke powder Particle size requirements: 74 μm≤coke powder particle diameter≤100 μm.
8. the method that a kind of agglomeration process according to claim 1-7 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: step 2: what subparticle was reunited concretely comprises the following steps:
Described exhaust gases passes is the flue collector (1) of sintering flue gas, flue collector (1) is provided with atomization agglomeration device (2), spraying into vaporific reunion liquid mist in atomization agglomeration device (2) to drip, the fine particle in flue gas is grown up in atomization agglomeration device (2) reunion nucleation, collision with reunion liquid.
9. the method that a kind of agglomeration process according to claim 8 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: the mist droplet particle size of the reunion liquid sprayed into is 30-150 μm, and the straying quatity of liquid of reuniting in every cubic metre of sintering flue gas is 10-20ml.
10. the method that a kind of agglomeration process according to claim 9 suppresses the discharge of Ore Sintering Process fine particle, it is characterised in that: atomization agglomeration device (2) includes collapsible tube (21), Cylindrical connecting tube (22) and expansion pipe (23).
Priority Applications (1)
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106590811A (en) * | 2016-11-22 | 2017-04-26 | 中冶节能环保有限责任公司 | Method for significantly reducing discharge of sintering flue gas inhalable particles and fine particles |
| CN106582185A (en) * | 2016-12-29 | 2017-04-26 | 潍坊学院 | Method for removing particulate matters from gas |
| CN107096350A (en) * | 2017-04-26 | 2017-08-29 | 华中科技大学 | It is a kind of to cooperate with the chemical agglomeration promotor and method for removing coal-fired flue-gas pollutant |
| CN107596838A (en) * | 2017-10-19 | 2018-01-19 | 哈尔滨工业大学（威海） | The spraying bionical reunion dust arrester of vibrating compound |
| WO2018018573A1 (en) * | 2016-07-29 | 2018-02-01 | 国电新能源技术研究院 | Method for removing fine particulate matters in flue gas of coal-fired power plant |
| CN107813760A (en) * | 2017-10-09 | 2018-03-20 | 何昌胜 | Full-automatic multi-functional auto-safety mechanism |
| CN109569169A (en) * | 2016-11-30 | 2019-04-05 | 安徽工业大学 | A kind of sintering flue gas fine particle capturing device and capture method |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101513583A (en) * | 2009-02-16 | 2009-08-26 | 华中科技大学 | Coal-fired ultrafine grain chemical agglomeration promotor |
| CN101837213A (en) * | 2009-03-16 | 2010-09-22 | 张顺 | Filter medium and preparation method thereof |
| CN102416363A (en) * | 2011-12-16 | 2012-04-18 | 江苏瑞帆环保装备股份有限公司 | Dust removal method and device based on chemical agglomeration and split linked anode electric dust removal |
| CN103405987A (en) * | 2013-09-02 | 2013-11-27 | 三门峡中兴煤炭综合利用研究开发中心 | Raised dust suppression method for semi-coke of upgraded lignite |
| CN104474830A (en) * | 2014-12-12 | 2015-04-01 | 广东电网有限责任公司电力科学研究院 | Chemical agglomeration promoter for removing fire coal fine particulate matters and application method of chemical agglomeration promoter |
-
2016
- 2016-04-28 CN CN201610288689.1A patent/CN105797531B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101513583A (en) * | 2009-02-16 | 2009-08-26 | 华中科技大学 | Coal-fired ultrafine grain chemical agglomeration promotor |
| CN101837213A (en) * | 2009-03-16 | 2010-09-22 | 张顺 | Filter medium and preparation method thereof |
| CN102416363A (en) * | 2011-12-16 | 2012-04-18 | 江苏瑞帆环保装备股份有限公司 | Dust removal method and device based on chemical agglomeration and split linked anode electric dust removal |
| CN103405987A (en) * | 2013-09-02 | 2013-11-27 | 三门峡中兴煤炭综合利用研究开发中心 | Raised dust suppression method for semi-coke of upgraded lignite |
| CN104474830A (en) * | 2014-12-12 | 2015-04-01 | 广东电网有限责任公司电力科学研究院 | Chemical agglomeration promoter for removing fire coal fine particulate matters and application method of chemical agglomeration promoter |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018018573A1 (en) * | 2016-07-29 | 2018-02-01 | 国电新能源技术研究院 | Method for removing fine particulate matters in flue gas of coal-fired power plant |
| CN106590811A (en) * | 2016-11-22 | 2017-04-26 | 中冶节能环保有限责任公司 | Method for significantly reducing discharge of sintering flue gas inhalable particles and fine particles |
| CN106590811B (en) * | 2016-11-22 | 2018-03-20 | 中冶节能环保有限责任公司 | A kind of method for substantially reducing sintering flue gas pellet and fine particle discharge |
| CN109569169B (en) * | 2016-11-30 | 2023-09-19 | 安徽工业大学 | Device and method for capturing fine particles of sintering flue gas |
| CN109569169A (en) * | 2016-11-30 | 2019-04-05 | 安徽工业大学 | A kind of sintering flue gas fine particle capturing device and capture method |
| CN106582185A (en) * | 2016-12-29 | 2017-04-26 | 潍坊学院 | Method for removing particulate matters from gas |
| CN107096350A (en) * | 2017-04-26 | 2017-08-29 | 华中科技大学 | It is a kind of to cooperate with the chemical agglomeration promotor and method for removing coal-fired flue-gas pollutant |
| CN107096350B (en) * | 2017-04-26 | 2019-05-14 | 华中科技大学 | A kind of chemical agglomeration promotor and method of collaboration removal coal-fired flue-gas pollutant |
| CN107813760A (en) * | 2017-10-09 | 2018-03-20 | 何昌胜 | Full-automatic multi-functional auto-safety mechanism |
| CN107596838A (en) * | 2017-10-19 | 2018-01-19 | 哈尔滨工业大学（威海） | The spraying bionical reunion dust arrester of vibrating compound |
| CN110215787A (en) * | 2019-05-31 | 2019-09-10 | 华电电力科学研究院有限公司 | A kind of sound wave strengthens fine particle removing device and removal methods |
| CN110215787B (en) * | 2019-05-31 | 2024-02-27 | 华电电力科学研究院有限公司 | Acoustic wave reinforced fine particulate matter removing device and removing method |
| CN114476731A (en) * | 2021-12-24 | 2022-05-13 | 武汉天空蓝环保科技有限公司 | Dry slag bin cooling dust fall waste gas emission reduction device and dry slag processing system |
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