CN101332410A - Exhaust gas treatment device and exhaust gas treatment method - Google Patents
Exhaust gas treatment device and exhaust gas treatment method Download PDFInfo
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- CN101332410A CN101332410A CNA2008101449794A CN200810144979A CN101332410A CN 101332410 A CN101332410 A CN 101332410A CN A2008101449794 A CNA2008101449794 A CN A2008101449794A CN 200810144979 A CN200810144979 A CN 200810144979A CN 101332410 A CN101332410 A CN 101332410A
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Abstract
An exhaust gas treatment system is provided that can sufficiently remove pollutants such as SO3 contained in combustion exhaust gas at low cost. In the exhaust gas treatment system for removing pollutants such as SO3 contained in combustion exhaust gas, there is provided dissolved salt aqueous solution sprays 35A, 35B, and 35C, that spray an Na2SO4 aqueous solution obtained from desulfurization effluent of a wet desulfurization system, into a flue though which the combustion exhaust gas flows.
Description
The application is that denomination of invention is dividing an application of " exhaust gas treatment device and exhaust gas treatment method ", and its applying date is on April 24th, 2006, and application number is 200610077716.7.
Technical field
The present invention relates to be used to remove for example SO
3Exhaust gas treatment device and exhaust gas treatment method Deng the polluter in the burning and gas-exhausting.
Background technology
Contain sulfur trioxide (SO in the burning and gas-exhausting that in combustion furnace, produces during for combustion of fossil fuels or rubbish etc.
3), hydrogen fluoride (HF), hydrogen chloride (HCl), mercury chloride (HgCl), hydrogen sulfide (H
2S), carbonyl sulfide polluters such as (COS).Therefore when these polluters are disposed in the atmosphere, can bring baneful influence, handle normal concentration according to requirements such as law or autonomous regulations or below it environment.In the past, the various exhaust gas treatment devices that are used to realize this processing had been proposed.
As an example of polluter, to SO
3Describe.
SO
3Mainly be the SO that produces by fuel (heavy oil or the coal etc.) burning that contains the sulphur composition
2Part oxidation and producing under hot environment.Therefore, SO
3Amount with respect to SO
2For about a few percent.But, because SO
3Become the reason of obstruction, corrosion or the boiler flue corrosion of air heater, and in the reason that is becoming purple cigarette (blueish smoke) when chimney cooling is discharged, therefore expectation is suppressed at several ppm with concentration of emission or below a few ppm.
As removing SO
3Method, known ammonia is blown into ammonia injection method in the burning and gas-exhausting.
The ammonia injection method produce as with the ammonium sulfate or the coal dust of the product of burning and gas-exhausting.Ammonium sulfate generally reclaims as solid by the dry type electrostatic (electric dust) precipitator, but the heavy metal class that is contained in the fuel such as heavy oil also is recovered simultaneously with ammonium sulfate, therefore be necessary to carry out the processing of other approach before in being discharged into environment, in this, the ammonia injection method has shortcoming on aspect cost of equipment and the operating cost.
In addition, for generating ammonium sulfate, inject ammonia in a large number, therefore, ammonia can be sneaked in the desulfurization draining of the wet desulfurizer that is arranged on the downstream.At this moment, for satisfying environmental standard, be necessary the desulfurization draining is handled.
In addition, ammonia needs sustainable supply, therefore because a large amount of consumption of ammonia hinder the reduction of operating cost.
On the other hand, inject the coal dust of generation or the ash of burning and gas-exhausting, electric dust collecting means or dielectric cleaning gas cleaning device (patent documentation 1) will be set in the downstream of flue sometimes for removing by ammonia.
[patent documentation 1]
No. 3564366 communique of patent
Summary of the invention
The problem that invention will solve
Electric dust collecting means or dielectric cleaning gas cleaning device are also removed SO when removing coal dust
3But, even use these, with the SO of high concentration
3When removing object, in the electric dust collecting means or dielectric cleaning gas cleaning device that use the processing capacity of setting up economically, fully capture SO
3Be difficult.
The present invention carries out in view of above situation, and its purpose is, providing can be cheap and remove the contained SO of burning and gas-exhausting fully
3Exhaust gas treatment device and exhaust gas treatment method Deng polluter.
Solve the method for problem
For solving above-mentioned problem, exhaust gas treatment device of the present invention and exhaust gas treatment method adopt following method.
Promptly, the exhaust gas treatment device that the present invention relates to is an exhaust gas treatment device of removing polluters such as sulfur trioxide contained in the burning and gas-exhausting, hydrogen fluoride, hydrogen chloride, mercury chloride, hydrogen sulfide, carbonyl sulfide, and this device has spray the sprayer unit that contains the aqueous solution of the dissolving salt of any chloride, hydroxide, sulfate or carbonate among Na, K, Mg, the Ca in the flue of above-mentioned burning and gas-exhausting circulation.
What present inventors furtherd investigate found that, if contain among Na, K, Mg, the Ca sulfate of any or the aqueous solution of the dissolving salt of carbonate, then can remove polluters such as sulfur trioxide, hydrogen fluoride, hydrogen chloride, mercury chloride, hydrogen sulfide, carbonyl sulfide effectively.
Containing among Na, K, Mg, the Ca sulfate of any or the aqueous solution of the dissolving salt of the carbonate reaction product of some treatment process (for example as) can be than being easier to and obtaining at an easy rate.Therefore, do not use the expensive soup just can be simply and implement pump-down process at an easy rate.
As dissolving salt, can enumerate NaCl, NaOH, Na
2SO
4, Na
2CO
3, KCl, KOH, K
2SO
4, K
2CO
3, KHCO
3, MgCl
2, MgSO
4, CaCl
2
As sulfur oxide contained in the burning and gas-exhausting, remove SO
3Can also enumerate SO outward,
2, but the present invention is particularly suitable for SO
3Processing, be not to remove SO
2Invention.
In addition,, can enumerate representational sulfur trioxide, but also go for polluter in addition as polluter.For example, hydrogen fluoride (HF), hydrogen chloride (HCl), mercury chloride (HgCl), hydrogen sulfide (H
2S), carbonyl sulfide (COS) etc.
As sprayer unit, see preferred two-fluid spray nozzle can making on the drop miniaturization this point of spraying.
As the mechanism of removing polluter, roughly consider as follows.
The aqueous solution that contains dissolving salt, by spraying become miniaturization drop, this miniaturization the dissolving salt of drop around moisture, evaporate by burning and gas-exhausting.Like this, make miniaturization the water evaporates of drop, and the dissolving salt particle that forms dry, thus can obtain miniaturization the dissolving salt particle.And, because SO
3Deng polluter with miniaturization drying the dissolving salt particle contact polluter adsorption of immobilization, and from gas, being removed.
That is, contain the aqueous solution of dissolving salt by spraying, it is little to form volume, and, the dry dissolving salt particle that quantity is many, thus can guarantee to be contained SO in the absorption burning and gas-exhausting
3Deng the necessary surface area of polluter, thereby reach the adsorption of immobilization purpose that promotes polluter.
Have, preferably, above-mentioned exhaust gas treatment device has wet desulfurizer again, and the above-mentioned aqueous solution is the desulfurization draining of above-mentioned wet desulfurizer.
As wet desulfurizer, when using soda process or magnesium hydroxide method, contain Na in the desulfurization draining as the sulfate of Na or Mg
2SO
4Or MgSO
4By such desulfurization draining is sprayed, can not consume new soup and remove SO
3Deng polluter.Thus, very cheap pump-down process becomes possibility.
Have again, above-mentioned exhaust gas treatment device, the outlet temperature of above-mentioned sprayer unit is set to more than 130 ℃ or 130 ℃, and is preferred more than 140 ℃ or 140 ℃.
Owing to be necessary to make moisture evaporation during the drop of the aqueous solution of spraying disperses, therefore preferably be set to the above environment of evaporation of water temperature or this temperature.In addition, preferably be set to SO with dissolving salt reaction
3Deng the dew-point temperature of polluter or this is more than temperature.When becoming the following temperature of dew-point temperature or this temperature, SO for example
3Gas becomes SO
3Mist, the absorption on the minuteness particle of the dissolving salt that this will be difficult to be implemented in dry makes and removes ability drop.Therefore, the outlet temperature of sprayer unit is set to more than 130 ℃ or 130 ℃, and is preferred more than 140 ℃ or 140 ℃.
And, as the drop of the aqueous solution of spraying, preferably become the diameter that moisture is evaporated during the drop of the aqueous solution of spraying disperses, for example, preferred 10 μ m～100 μ m, the more preferably diameter about 20 μ m～50 μ m.
Have, exhaust gas treatment device of the present invention has the air heater that adds the air of heat supply combustion furnace by the heat that obtains from burning and gas-exhausting again, and above-mentioned sprayer unit is arranged on the upstream side of above-mentioned air heater.
For example, when containing sulfur trioxide in the burning and gas-exhausting, can be because the sulfuric acid that generates because of sulfur trioxide corrodes air heater.Among the present invention,, polluters such as sulfur trioxide are removed, prevented the corrosion of air heater at the upstream side of air heater by sprayer unit being arranged on the upstream side of air heater.
In addition, because the upstream side of air heater is in the front of capturing the sensible heat of burning gases by air heater, therefore can keep than higher temperature (for example, 300～350 ℃).Therefore, promote the evaporation of moisture of the drop of spraying, improve the efficient of removing of polluter.
Have again, exhaust gas treatment device of the present invention have by the heat that obtains from burning and gas-exhausting add heat supply give combustion furnace air air heater and be arranged on the electric dust collecting means in this air heater downstream, above-mentioned sprayer unit is arranged between above-mentioned air heater and the above-mentioned electric dust collecting means.
For example, when containing sulfur trioxide in the burning and gas-exhausting, by the sulfuric acid corrosion electric dust collecting means that generates by sulfur trioxide.Among the present invention,, polluter is removed, prevented the corrosion of electric dust collecting means at the upstream side of electric dust collecting means by sprayer unit being arranged between above-mentioned air heater and the above-mentioned electric dust collecting means.
In addition, remove the method for sulfur trioxide and compare with inject ammonia at the upstream side of electric dust collecting means, and burning and gas-exhausting in polluter between the processing of the product that generates simple.That is to say, in the ammonia injection method, need the operation of other approach to handle contained heavy metal class in the ammonium sulfate that generates as product.In the present invention, do not use ammonia, and use dissolving salt (for example, the Na contain among Na, K, Mg, the Ca any
2SO
4Or MgSO
4), therefore do not need to handle the operation of ammonium sulfate.In addition, owing to do not use the ammonia injection method, therefore can suppress the generation of coal dust.
Have again, according to exhaust gas treatment device of the present invention, have heat heating by obtaining from burning and gas-exhausting supply to combustion furnace air air heater and be arranged on the electric dust collecting means in this air heater downstream and be arranged on the wet desulfurizer in this electric dust collecting means downstream, above-mentioned sprayer unit is arranged between above-mentioned electric dust collecting means and the above-mentioned wet desulfurizer and near this wet desulfurizer.
Owing to use dissolving salt, and burning and gas-exhausting in polluter between the product that generates be easy to be dissolved in the desulfurization draining of wet desulfurizer.In addition, because sprayer unit is arranged near the wet desulfurizer, so product flows into the reservoir of the desulfurization draining of wet desulfurizer.The product that flows into the reservoir of desulfurization draining is dissolved in the desulfurization draining, and processed with the desulfurization draining.Therefore, do not need to be provided with separately the treatment process of product, can simplified apparatus.
For example, in the situation of the wet desulfurizer that uses soda process, use Na
2SO
4During as dissolving salt, the SO in the burning and gas-exhausting
3By adsorption of immobilization in miniaturization the dissolving salt particle of drying on and from gas, remove.In addition, the dissolving salt particle (Na by drying
2SO
4) a part and SO
3Carry out the following formula reaction, generate NaHSO
4H
2O (solid).Here, because NaSO
4And NaHSO
4H
2O is deliquescent, therefore dissolves in the desulfurizer of downstream (back stream).
Na
2SO
4+SO
3+3H
2O→2NaHSO
4·H
2O
Like this, has the advantage that does not need the such solids of ammonia injection method to handle.
In addition, exhaust gas treatment device of the present invention have by the heat that obtains from burning and gas-exhausting add the heat supply combustion furnace air air heater and be arranged on the electric dust collecting means in this air heater downstream and be arranged on the wet desulfurizer in this electric dust collecting means downstream, above-mentioned sprayer unit is arranged between the upstream side of above-mentioned air heater, above-mentioned air heater and the above-mentioned electric dust collecting means, near between above-mentioned electric dust collecting means and the above-mentioned wet desulfurizer and any 2 places in this wet desulfurizer.
By sprayer unit being set, can reduce the concentration of polluter significantly at 2 places.
In addition, if a spray position is arranged on the upstream side of air heater, then the burning and gas-exhausting temperature of air heater upstream side is owing to can keep high temperature by the combustion furnace of its upstream side, thus, can prevent the reduction of the burning and gas-exhausting temperature in downstream, can keep to heavens than the air heater organic efficiency of the polluter of the spray position in downstream more.
Have, exhaust gas treatment device of the present invention has wet type electric dust collecting means or dielectric cleaning gas cleaning device again.
By wet type electric dust collecting means or dielectric cleaning gas cleaning device, also can remove the polluter in the burning and gas-exhausting, therefore can be with the equipment miniaturization of following the sprayer unit of dissolving salt spraying.
Because dielectric cleaning gas cleaning device is being removed SO
3On excellent especially, therefore, be fit to remove SO
3Situation for purpose.
In addition, exhaust gas treatment method of the present invention is an exhaust gas treatment method of removing polluters such as sulfur trioxide contained in the burning and gas-exhausting, hydrogen fluoride, hydrogen chloride, mercury chloride, hydrogen sulfide, carbonyl sulfide, this method is that spraying contains the aqueous solution of the dissolving salt of any chloride, hydroxide, sulfate or carbonate among Na, K, Mg, the Ca in the flue of above-mentioned burning and gas-exhausting circulation.
The aqueous solution reaction product of some treatment process (for example as) that contains the dissolving salt of any chloride, hydroxide, sulfate or carbonate among Na, K, Mg, the Ca can be than being easier to and obtaining at an easy rate.Therefore, can be simply and implement pump-down process at an easy rate.
As dissolving salt, can enumerate NaCl, NaOH, Na
2SO
4, Na
2CO
3, KCl, KOH, K
2SO
4, K
2CO
3, KHCO
3, MgCl
2, MgSO
4, CaCl
2
As sulfur oxide contained in the burning and gas-exhausting, remove SO
3Can also enumerate SO outward,
2, but the present invention is particularly suitable for SO
3Processing, be not to remove SO
2Invention.
In addition,, can enumerate representational sulfur trioxide, but also go for polluter in addition as polluter.For example, hydrogen fluoride (HF), hydrogen chloride (HCl), mercury chloride (HgCl), hydrogen sulfide (H
2S), carbonyl sulfide (COS) etc.
As the mechanism of removing polluter, roughly consider as follows.
The aqueous solution that contains dissolving salt, by spraying become miniaturization drop, this miniaturization the dissolving salt of drop around moisture, evaporate by burning and gas-exhausting.Like this, make miniaturization the water evaporates of drop, and the dissolving salt particle that forms dry, thus can obtain miniaturization the dissolving salt particle.And, because SO
3Deng polluter with miniaturization drying the dissolving salt particle contact polluter adsorption of immobilization, and from gas, being removed.
That is, contain the aqueous solution of dissolving salt by spraying, it is little to form volume, and, the dry dissolving salt particle that quantity is many, thus can guarantee to be contained SO in the absorption burning and gas-exhausting
3Deng the necessary surface area of polluter, thereby reach the adsorption of immobilization effect that promotes polluter.
The invention effect
According to the present invention, can realize following effect.
Owing to use the aqueous solution of the dissolving salt of the sulfate contain among Na, K, Mg, the Ca any or carbonate, can remove SO
3Deng polluter, therefore need not inject expensive medicament, just can carry out pump-down process.
In addition, if supply with the above-mentioned aqueous solution, can carry out pump-down process at an easy rate with simple formation by the desulfurization draining.
The simple declaration of accompanying drawing
Fig. 1 is the synoptic diagram that the exhaust gas treatment device that the 1st embodiment of the present invention relates to is shown.
Fig. 2 is the synoptic diagram that the exhaust gas treatment device that the 2nd embodiment of the present invention relates to is shown.
Fig. 3 is the synoptic diagram that the variation example of Fig. 2 is shown.
Fig. 4 illustrates to carry out SO
3Remove the synoptic diagram of experimental rig.
Fig. 5 illustrates to carry out SO
3Remove the curve map of result of the test.
Fig. 6 illustrates to carry out SO
3Remove the curve map of result of the test.
Symbol description
1A, 1B: exhaust gas treatment device
5: flue
9: air heater
11: the dry type electric dust collecting means
13: wet desulfurizer
15: dielectric cleaning gas cleaning device
35A, B, C: dissolving salt sprayer (sprayer unit)
The preferred plan that carries out an invention
Below, with reference to accompanying drawing, the embodiment that the present invention relates to is described.
[the 1st embodiment]
Below, with Fig. 1 the 1st embodiment of the present invention is described.
The present embodiment is the exhaust gas treatment device that is suitable for the wet desulfurizer that uses soda process.
Fig. 1 illustrates the exhaust gas treatment device that the present embodiment relates to.
Exhaust gas treatment device 1A has: denitrogenation (denitration) device 7 and air heater 9 and dry type electric dust collecting means 11 and wet desulfurizer 13 and dielectric cleaning gas cleaning device 15 and the chimney 17 that are arranged on the flue 5 in boiler (combustion furnace) 3 downstreams.
Nitrogen rejection facility 7 is devices of removing the nitrogen oxide (NOx) that contains in the burning and gas-exhausting of discharging from boiler 3.
Dry type electric precipitation machine 11 is the devices that capture the coal dust in the burning and gas-exhausting by electrostatic force.
Be provided with absorbent supply pump 26 between absorbent sprayer 20 and the reservoir 24, by the absorbent solution in these absorbent supply pump 26 extraction reservoir 24.
NaOH solution is supplied to reservoir 24 from NaOH solution feedway 24a, and air is supplied to reservoir 24 by air feeder 24b.
From the absorbent solution of sprayer 20 ejections, in packed layer 22, the SO in the burning and gas-exhausting
2Be absorbed in the absorbent solution.Be absorbed in the SO of absorbent solution
2Become NaHSO
3, by generating Na with the reaction of oxygen
2SO
4Contain this Na
2SO
4The desulfurization draining be discharged to the outside by discharge pipe 28.
SO
3Not in wet desulfurizer 13 with absorbent solution generation chemical reaction, by with the collision and the aggegation of the particulate of absorbent solution, though be micro-, but also can remove.
Dielectric cleaning gas cleaning device 15 is that the dielectric particles such as water that will spray carry out dielectric polarization, captures charged in advance coal dust or SO by the Coulomb force that acts between each insulating particles
3
In addition, also can use the wet type electric dust collecting means to replace dielectric cleaning gas cleaning device 15.
In the present invention, for removing SO
3, use the desulfurization draining of storing in the reservoir 24 of wet desulfurizer 13.
Mainly contain Na in the desulfurization draining as dissolving salt
2SO
4The Na that is dissolved in the water
2SO
4The aqueous solution also contains the NaOH solution that NaOH solution feedway 24a supplies with that passes through partly.
The desulfurization draining is by draw-off pump 32, delivers to the upstream side of wet desulfurizer 13 by extraction tube 30, by dissolving salt sprayer (sprayer unit) 35A, B, C at flue 5 internal sprayings.The desulfurization draining is preferably by being made the two-fluid spray nozzle of liquid particleization spray by forced air.The desulfurization draining of spraying preferably is set to 10 μ m～100 μ m, more preferably 20 μ m～50 μ m, the further diameter of preferred 25 μ m～35 μ m.
By Na contained in the desulfurization draining
2SO
4The aqueous solution, the SO in the burning and gas-exhausting
3Since be absorbed and fixed at miniaturization drying the dissolving salt particle on, then from gas, remove.In addition, by drying dissolving salt particle (Na
2SO
4) a part and SO
3Carry out the following formula reaction, generate NaHSO
4H
2O (solid).Here, because NaSO
4And NaHSO
4H
2O is deliquescent, therefore dissolves in the desulfurizer of downstream (back stream).
Na
2SO
4+SO
3+2H
2O→2NaHSO
4·H
2O
In addition, by the NaOH aqueous solution contained in the desulfurization draining, remove the SO in the burning and gas-exhausting
2
The position of desulfurization draining spraying can be from the position C between the position B between the position A between nitrogen rejection facility 7 and the air heater 9, air heater 9 and the dry type electrostatic (electric dust) precipitator 11, dry type electrostatic (electric dust) precipitator 11 and the wet desulfurizer 13 any one in selected.Certainly, also can while select location A and position B or position A and 2 such places of position C.
The temperature of position A is about 300～350 ℃, and the temperature of position B is about 160～200 ℃, and the temperature of position C is about 160～200 ℃.
Select the advantage of each position A～C as follows.
When the spray position of desulfurization draining is chosen to be position A as the upstream of air heater 9, SO
3Upstream at air heater 9 is removed, and therefore, can prevent the corrosion to air heater 9 of the sulfuric acid that produced by the sulfur trioxide in the burning and gas-exhausting.
In addition, because the upstream side of air heater 9 is the fronts of capturing the sensible heat of burning and gas-exhausting by air heater 9, therefore can keep than higher temperature (for example, 300～350 ℃).Therefore, the Na in the desulfurization draining that promotes to spray
2SO
4The water evaporates of aqueous solution particle improves SO
3Remove efficient.
Because position B is arranged on the upstream of dry type electric dust collecting means 11,, can prevent by the corrosion of the sulfuric acid of the generation of the sulfur oxide in the burning and gas-exhausting to dry type electric dust collecting means 11 therefore by the spraying of desulfurization draining.
In addition, with respect to the ammonia injection method that used in the past, capture SO
3After the processing of product become simple.That is, when the desulfurization draining was sprayed, product became water miscible sulfate, handled the ammonia injection method of the operation of the solid product contain ammonium sulfate or heavy metal class with respect to needs, handled and became very simple.That is, the processing of product can with wet desulfurizer 13 generalizations, equipment cost can be suppressed at low-level.In addition, in the ammonia injection method,,,, also be favourable still handling on the easy this point though produce coal dust as product if adopt the desulfurization draining spraying of soda process as the ammonium sulfate ash that produces as the processing complexity of product.
Position C is owing to be arranged near the wet desulfurizer 13, therefore, and with SO
3Product and the air-flow of burning and gas-exhausting flow to the downstream together, flow into reservoir 24.Therefore, the product that is produced by the desulfurization draining from position C spraying is captured by wet desulfurizer 13, then, handles with the desulfurization draining, can be with the generalization of desulfurization drainage treatment equipment.
In addition, if the position of desulfurization draining spraying is chosen to be position A and position B or position A and position C, can reduce SO significantly
3Concentration.For example, only can not remove SO below the concentration at the safe level of position A or this
3The time, can establish desulfurization draining sprayer unit at position B or position C benefit.
If spray position is set to the position A as air heater 9 upstream sides, since the temperature of air heater 9 upstream sides can be by its upstream side the ability control of boiler 3 maintain the temperature of regulation, therefore, can prevent the reduction of the temperature of the burning and gas-exhausting that produces by desulfurization draining spraying as much as possible.Therefore, than air heater 9 more the reduction of the burning and gas-exhausting temperature of the position B in downstream or position C lack, can be maintained and remove SO
3Necessary temperature levels.
The exhaust gas treatment device 1A of above-mentioned formation uses as follows.
Describe as an example when in the following description, being arranged on position A and position B with the position of dissolving salt sprayer 35.
When burning contains the more heavy oil of sulphur composition in boiler 3, contain SO
2Burning and gas-exhausting be expelled to the flue 5 in downstream.SO
2A part (a few %) oxidized in the high-temperature portion of boiler 3 or nitrogen rejection facility 7, be converted into SO
3
At position A, by by the micronized desulfurization draining of dissolving salt sprayer 35A, SO
3Be removed major part.Here, contain Na by spraying as dissolving salt
2SO
4The desulfurization draining of the aqueous solution, SO
3Be adsorbed the drying that is immobilized in miniaturization the dissolving salt particle on, thereby from gas, remove.In addition, by drying dissolving salt particle (Na
2SO
4) a part and SO
3The following formula reaction generates NaHSO
4H
2O (solid).
Na
2SO
4+SO
3+2H
2O→2NaHSO
4·H
2O
In addition, the burning and gas-exhausting temperature of position A is set to 300～350 ℃.
Remove most SO
3Burning and gas-exhausting by air heater 9, bring the combustion air of supply and in-position B by forced ventilation 10 with the part of sensible heat.At this moment, the temperature of burning and gas-exhausting drops to about 160～200 ℃.
At position B, will spray by the micronized desulfurization draining of dissolving salt sprayer 35B again, further remove SO
3Follow SO in this wise
3Remove and the solid product that generates, the coal dust in exhaust is captured by dry type electric dust collecting means 11, and is discharged to the outside.
Remove most of SO at position A and position B
3Burning and gas-exhausting, flow into wet desulfurizer 13.
In wet desulfurizer 13, by removing SO by the absorbent solution of absorbent sprayer 20 sprayings
2In reservoir 24, NaOH and SO
2Reaction generates Na
2SO
4Na
2SO
4The solubility height, its part is with Na
2SO
4The state of the aqueous solution is expelled to the outside by discharge pipe 28.On the other hand, other Na
2SO
4The aqueous solution is drawn out of by draw-off pump 32, by extraction tube 30, is delivered among each dissolving salt sprayer 35A, B.
In wet desulfurizer 13, removed SO
2Burning and gas-exhausting guiding dielectric cleaning gas cleaning device 15, remove remaining coal dust and SO at this
3Deng after, be discharged into the outside from chimney 17.
According to the present embodiment, can realize following action effect.
By spraying Na
2SO
4The aqueous solution makes the drop of miniaturization, makes the Na of the drop of this miniaturization again by burning and gas-exhausting
2SO
4Water evaporates on every side.So, then obtain the Na of miniaturization
2SO
4Particle, and make SO
3Na with this miniaturization
2SO
4The particle contact is so that SO
3Adsorption of immobilization reaches the purpose of removing from gas.That is, by spraying Na
2SO
4The aqueous solution has realized that then the formation volume is little, and, the dry Na that quantity is many
2SO
4The purpose of particle.Therefore guaranteed to be contained SO in the absorption burning and gas-exhausting
3Necessary surface area, thus SO can be promoted
3Adsorption of immobilization.
Because by Na as dissolving salt
2SO
4The aqueous solution is removed SO
3, therefore, only supply with Na by the desulfurization draining
2SO
4The aqueous solution gets final product, and does not need to inject new medicament.Therefore, can and remove SO at an easy rate with very simple formation
3
Because Na
2SO
4And SO
3Reaction product solubility height, therefore, can be with the state processing of the aqueous solution.So, compare with the ammonia injection method that needs solids to handle, handle very simple.
For removing SO
3, owing to needn't adopt the ammonia injection method, therefore, do not need to handle the equipment of the product that produces by the ammonia injection method, reduced cost.In addition, owing to do not need the sustainable supply ammonia, so, operating cost can be suppressed at low-level.
Owing to adopt carrying out the desulfurization draining two stages and spray as position A and position B, therefore, can reduce SO significantly
3Concentration.
In addition, by with the SO that can remove ormal weight
3The combination of dielectric cleaning gas cleaning device 15, can reduce the SO that uses the desulfurization draining
3Treating capacity, thereby can closely constitute equipment from extraction tube 30 to dissolving salt sprayer 35A, B, C.
In addition, in the present embodiment, for obtaining Na
2SO
4The aqueous solution and use the desulfurization draining, but make Na separately
2SO
4The aqueous solution, A～C sprays it from the position, also can remove SO
3
In addition, in the present embodiment, describe as an example, adopt Mg (OH) but equally also go for using with the wet desulfurizer 13 that uses soda process
2The wet desulfurizer of magnesium hydroxide method.At this moment, with MgSO contained in the desulfurization draining
4As being used to remove SO
3The dissolving salt utilization.
In addition, as dissolving salt, enumerated Na
2SO
4Or MgSO
4, but so long as the sulfate of any one among Na, K, Mg, the Ca or the dissolving salt of carbonate can be removed SO
3Deng polluter.
In addition, as an example of the polluter of removing, used SO
3, but can also remove hydrogen fluoride (HF), hydrogen chloride (HCl), mercury chloride (HgCl), hydrogen sulfide (H
2S), carbonyl sulfide (COS) etc.
[the 2nd embodiment]
Below, use Fig. 2 that the 2nd embodiment of the present invention is described.
The present embodiment is the exhaust gas treatment device that is applicable to the wet desulfurizer that adopts the lime stone-gypsum method.
In addition, to giving prosign, and omit its explanation with the same inscape of the 1st embodiment.
Fig. 2 illustrates the exhaust gas treatment device that the present embodiment relates to.
Exhaust gas treatment device 1B uses the lime stone (CaCO that supplies with from lime stone feedway 24c
3) remove sulfur oxide as absorbent.Because the product that the lime stone-gypsum method produces is the CaSO of slightly solubility
4, therefore SO is removed in the use desulfurization draining that is difficult to carry out as in the 1st embodiment
3
Here, in the present embodiment, be provided with the 2nd wet desulfurizer 38 midway than the employing soda process of wet type desulfurizer 13 small scales at flue 5.The 2nd wet desulfurizer 38 has the 2nd reservoir 40 in wet desulfurizer 13 upstreams, and in the 2nd reservoir 40, NaOH solution feedway 40a is connected with air feeder 40b, and NaOH solution and air supply in the 2nd reservoir 40.The NaOH solution of supplying with the 2nd reservoir 40 is dissolved in the absorption liquid, by the 2nd absorbent supply pump 42 from the 2nd absorbent sprayer 44 at flue 5 internal sprayings.Contain the Na that in the 2nd reservoir 40, generates
2SO
4The desulfurization draining of the aqueous solution is delivered to the upstream side more of the 2nd absorbent sprayer 44 by draw-off pump 48 by extraction tube 46, by dissolving salt sprayer (sprayer unit) 35A, B, C at flue 5 internal sprayings.
In the present embodiment, be provided with the 2nd wet desulfurizer 38 of the employing soda process of small scale at the upstream side of the wet desulfurizer 13 that uses the lime stone-gypsum method, generate Na as dissolving salt
2SO
4, will mainly contain this Na
2SO
4The desulfurization draining of the aqueous solution is sprayed in the flue 5 of upstream side.Thus, manufacturing Na needn't be set
2SO
4Large-scale equipment, just can supply with and be used to remove SO
3Na
2SO
4
In addition, the 2nd wet desulfurizer 38 is so long as can obtain to be used to remove SO
3The Na of necessary amount
2SO
4The scale of degree get final product.Because the SO in the burning and gas-exhausting
3Amount be SO
2Several %, therefore the 2nd wet desulfurizer 38 gets final product for the scale of dwindling significantly than wet type desulfurizer 13.
In addition, as shown in Figure 3, replace the 2nd wet desulfurizer 38 that is arranged at flue 5 Fig. 2 midway, the 3rd wet desulfurizer 50 of small-scale employing soda process also can be set outside flue 5.At this moment, branched pipe 52 is connected on the flue 5, the part of burning and gas-exhausting is imported the 3rd wet desulfurizer 50.In the 3rd wet desulfurizer 50, similarly carry out desulfurization with the 2nd wet desulfurizer 38, generate in the 3rd reservoir 54 and contain Na
2SO
4The desulfurization draining of the aqueous solution.The desulfurization draining is transported among dissolving salt sprayer (sprayer unit) 35A, B, the C by extraction tube 58 by by drawing pump 56.
In addition, in the present embodiment,, use soda process, but also can use the magnesium hydroxide method as the 2nd wet desulfurizer 38 and the 3rd wet desulfurizer 50.
In addition, as dissolving salt, be not only Na
2SO
4Or MgSO
4, and, so long as the sulfate of any one among Na, K, Mg, the Ca or the dissolving salt of carbonate then can be removed SO
3Deng polluter.
In addition, as an example of the polluter of removing, used SO
3, but can also remove hydrogen fluoride (HF), hydrogen chloride (HCl), mercury chloride (HgCl), hydrogen sulfide (H
2S), carbonyl sulfide (COS) etc.
In addition, also can not use the 2nd wet desulfurizer 38 and the 3rd wet desulfurizer 50, directly each position A～C be supplied with Na
2SO
4The aqueous solution or MgSO
4The aqueous solution.
[embodiment]
Use Fig. 4～Fig. 6, to removing SO
3Test describe.
The summary of experimental rig has been shown among Fig. 4.
Upstream side at cooling tower 103 is provided with the dissolving salt sprayer 115 that uses two-fluid spray nozzle.The ejection diameter is about the drop of 20 μ m from dissolving salt sprayer 115.
Between LPG stove 101 and the cooling tower 103 SO is set
3 Feedway 107 thus, is adjusted initial SO
3Concentration.
In the inlet of cooling tower 103, the upstream side of water spray device 113a, b and the outlet of cooling tower 103 temperature sensor is set.In addition, in the inlet of cooling tower 103, the outlet of cooling tower 103 and the outlet of electric dust collecting means 105 SO is set
3Concentration sensor.
Test in the present embodiment is set to 185 ℃, the SO of the inlet of cooling tower 103 in the inlet temperature of cooling tower 103
3Concentration is set to carry out under the condition of 170ppm.
Fig. 5 illustrates the result of the test of using above-mentioned experimental rig 100.In Fig. 5, transverse axis is supplied with concentration [wt%] for the dissolving salt aqueous solution, and the longitudinal axis is the SO of cooling tower 103 outlets
3Concentration [ppm].
In the present embodiment, use employing Na
2SO
4, MgSO
4And NaOH is as the aqueous solution and the soda process desulfurization draining of dissolving salt.
As shown in Figure 5, will be by SO
3The initial stage SO that feedway 107 is adjusted
3When concentration is set to 170ppm, use any dissolving salt aqueous solution can be with SO
3Remove and to go to about 60ppm or below the 60ppm.Therefore, if SO is set in the downstream
3The rate of removing is about 90% electric dust collecting means or dielectric cleaning gas cleaning device, can be with SO
3Concentration is reduced to several ppm, can prevent the generation of purple cigarette.
Fig. 6 shows and changes the Na of flow with 5wt%
2SO
4Result of the test when the aqueous solution is sprayed.Among this figure, transverse axis is Na
2SO
4Aqueous solution spray amount [L/hr], left side axle is the SO of cooling tower 103 outlets
3Concentration [ppm], right axle be the spray outlet temperature [℃].
With Na
2SO
4The rising of aqueous solution spray amount is proportional, and the spray outlet temperature demonstrates reduction.
Na
2SO
4Aqueous solution mist flow is 50[L/hr] time, that is, and when the spray outlet temperature is about 130 ℃, SO
3Concentration surpasses 60ppm slightly, but the spray outlet temperature is when being set to 140 ℃, SO
3Concentration reduces to 40ppm or below the 40ppm significantly.Therefore, vapo(u)rizing temperature is set to more than 130 ℃ or 130 ℃, and is preferred more than 140 ℃ or 140 ℃, can improve SO
3The rate of removing.
Claims (10)
1. exhaust gas treatment device, this device is to remove the exhaust gas treatment device that is selected from least a polluter in sulfur trioxide, hydrogen fluoride, hydrogen chloride, mercury chloride, hydrogen sulfide or the carbonyl sulfide contained in the burning and gas-exhausting, this device has:
In the flue of above-mentioned burning and gas-exhausting circulation, spray the sprayer unit of the aqueous solution of the chloride that contains among more than one Na, K, Mg, the Ca any or sulfate.
2. according to the described exhaust gas treatment device of claim 1, this device has wet desulfurizer, and the above-mentioned aqueous solution is the desulfurization draining of above-mentioned wet desulfurizer.
3. according to the described exhaust gas treatment device of claim 1, wherein, the outlet temperature of above-mentioned sprayer unit is more than 130 ℃ or 130 ℃.
4. according to the described exhaust gas treatment device of claim 1, wherein, the outlet temperature of above-mentioned sprayer unit is more than 140 ℃ or 140 ℃.
5. according to the described exhaust gas treatment device of claim 1, this device has the air heater that adds the air of heat supply combustion furnace by the heat that obtains from burning and gas-exhausting, and above-mentioned sprayer unit is arranged on the upstream side of above-mentioned air heater.
6. according to the described exhaust gas treatment device of claim 1, this device have by the heat that obtains from burning and gas-exhausting add the heat supply combustion furnace air air heater and be arranged on the electric dust collecting means in this air heater downstream, above-mentioned sprayer unit is arranged between above-mentioned air heater and the above-mentioned electric dust collecting means.
7. according to the described exhaust gas treatment device of claim 1, this device have by the heat that obtains from burning and gas-exhausting add the air of heat supply combustion furnace air heater, be arranged on the electric dust collecting means in this air heater downstream and be arranged on the wet desulfurizer in this electric dust collecting means downstream, above-mentioned sprayer unit is arranged between above-mentioned electric dust collecting means and the above-mentioned wet desulfurizer and near this wet desulfurizer.
8. according to the described exhaust gas treatment device of claim 1, this device have by the heat that obtains from burning and gas-exhausting add the air of heat supply combustion furnace air heater, be arranged on the electric dust collecting means in this air heater downstream and be arranged on the wet desulfurizer in this electric dust collecting means downstream, above-mentioned sprayer unit is arranged between the upstream side of above-mentioned air heater, above-mentioned air heater and the above-mentioned electric dust collecting means, near between above-mentioned electric dust collecting means and the above-mentioned wet desulfurizer and any 2 places in this wet desulfurizer.
9. according to the described exhaust gas treatment device of claim 1, this device has wet type electric dust collecting means or dielectric cleaning gas cleaning device.
10. exhaust gas treatment method, this method is to be used for removing the contained exhaust gas treatment method that is selected from least a polluter in sulfur trioxide, hydrogen fluoride, hydrogen chloride, mercury chloride, hydrogen sulfide or the carbonyl sulfide of burning and gas-exhausting, this method comprises:
Spraying contains among more than one Na, K, Mg, the Ca chloride of any or the aqueous solution of sulfate in the flue of above-mentioned burning and gas-exhausting circulation.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP128045/05 | 2005-04-26 | ||
| JP2005128045 | 2005-04-26 | ||
| JP052919/06 | 2006-02-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100777167A Division CN100475316C (en) | 2005-04-26 | 2006-04-24 | Exhaust gas treatment device and exhaust gas treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101332410A true CN101332410A (en) | 2008-12-31 |
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ID=37483094
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|---|---|---|---|
| CNB2006100777167A Active CN100475316C (en) | 2005-04-26 | 2006-04-24 | Exhaust gas treatment device and exhaust gas treatment method |
| CNA2008101449794A Pending CN101332410A (en) | 2005-04-26 | 2006-04-24 | Exhaust gas treatment device and exhaust gas treatment method |
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|---|---|
| CN (2) | CN100475316C (en) |
| TW (1) | TWI280152B (en) |
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|---|---|---|---|---|
| CN112378266A (en) * | 2020-11-10 | 2021-02-19 | 宁夏太阳镁业有限公司 | Magnesium metal is smelted and is used desulfurization system |
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| NZ597608A (en) * | 2009-07-16 | 2014-02-28 | Babcock & Wilcox Power Generat | Redox method for capture of total gaseous mercury by wet fgd |
| CN102343213B (en) * | 2011-10-13 | 2013-07-03 | 中冶赛迪工程技术股份有限公司 | Process and system for treating strong brine with flue gas desulfurizing device |
| TWI507685B (en) * | 2013-01-14 | 2015-11-11 | Univ Fooyin | Nitric oxide radiosonde |
| CN103861438B (en) * | 2014-02-22 | 2016-03-09 | 浙江大学 | The system and method for deep removal coal-fired flue-gas oxysulfide |
| CN104492244A (en) * | 2014-12-17 | 2015-04-08 | 国网上海市电力公司 | Waste-gas treating equipment |
| JP7128078B2 (en) * | 2018-10-12 | 2022-08-30 | 株式会社荏原製作所 | Abatement device, method for replacing piping of abatement device, and method for cleaning pipe of abatement device |
-
2005
- 2005-10-26 TW TW94137539A patent/TWI280152B/en active
-
2006
- 2006-04-24 CN CNB2006100777167A patent/CN100475316C/en active Active
- 2006-04-24 CN CNA2008101449794A patent/CN101332410A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112378266A (en) * | 2020-11-10 | 2021-02-19 | 宁夏太阳镁业有限公司 | Magnesium metal is smelted and is used desulfurization system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100475316C (en) | 2009-04-08 |
| TWI280152B (en) | 2007-05-01 |
| TW200637643A (en) | 2006-11-01 |
| CN1872395A (en) | 2006-12-06 |
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