CN204121971U - The flue gas desulfur device of a kind of low energy consumption, ultra-clean discharge - Google Patents
The flue gas desulfur device of a kind of low energy consumption, ultra-clean discharge Download PDFInfo
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- CN204121971U CN204121971U CN201420553295.0U CN201420553295U CN204121971U CN 204121971 U CN204121971 U CN 204121971U CN 201420553295 U CN201420553295 U CN 201420553295U CN 204121971 U CN204121971 U CN 204121971U
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 78
- 239000003546 flue gas Substances 0.000 title claims abstract description 78
- 238000005265 energy consumption Methods 0.000 title claims abstract description 24
- 239000002002 slurry Substances 0.000 claims abstract description 296
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 93
- 210000002966 serum Anatomy 0.000 claims abstract description 89
- 230000023556 desulfurization Effects 0.000 claims abstract description 67
- 238000005507 spraying Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 239000000779 smoke Substances 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims description 43
- 238000010521 absorption reaction Methods 0.000 claims description 27
- 230000003647 oxidation Effects 0.000 claims description 26
- 238000007254 oxidation reaction Methods 0.000 claims description 26
- 230000003009 desulfurizing effect Effects 0.000 claims description 23
- 239000006227 byproduct Substances 0.000 claims description 21
- 230000007246 mechanism Effects 0.000 claims description 14
- 230000005484 gravity Effects 0.000 claims description 8
- 238000000034 method Methods 0.000 abstract description 29
- 230000008569 process Effects 0.000 abstract description 14
- 239000007787 solid Substances 0.000 abstract description 13
- 230000009467 reduction Effects 0.000 abstract description 7
- 239000010440 gypsum Substances 0.000 description 36
- 229910052602 gypsum Inorganic materials 0.000 description 36
- 238000005406 washing Methods 0.000 description 12
- 230000009286 beneficial effect Effects 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- 230000001276 controlling effect Effects 0.000 description 6
- 238000002425 crystallisation Methods 0.000 description 6
- 230000008025 crystallization Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000004575 stone Substances 0.000 description 6
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000000151 deposition Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 230000002411 adverse Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 241001314440 Triphora trianthophoros Species 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000009885 systemic effect Effects 0.000 description 1
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Abstract
The utility model discloses the flue gas desulfur device of a kind of low energy consumption, ultra-clean discharge, belong to smoke pollution process field, desulfurization slurry is separated into two independently desulfurization sprayed slurry circulatory systems by the utility model, adopt the three-circulation desulphurization technique of two slurries gathering-device (slurry pool/case), two serum density, control zones of different slurry pH value, reach reduction energy consumption, meet PM, SO
2ultra-clean or near-zero release object.By the pH value arranging two slurry pool/case, control the different serum density of two slurry pool/case, control zones of different slurries, and form two independently serum recycle loops, the object that after realizing desulfurization, neat stress drop solid content is greater than 99% lower than 10% and system desulfuration efficiency; Arranged by the outer slurry tank high liquid level of tower, and less spraying layer, reach and reduce circulation pump power, reduction desulfurization operation power consumption object.
Description
Technical field
The utility model belongs to smoke pollution process field, particularly relates to means of flue gas desulfurization of power plant field.
Background technology
Wet Flue Gas Desulfurization Technology because technical maturity, desulfuration efficiency are higher, investment and operating cost lower, be widely used in flue gas desulphurization field.Wherein, wet desulfurization of flue gas by limestone-gypsum method technique due to development comparatively early, reliable, the desulfurizing agent cheaper starting materials of technology maturation is easy to get, and occupies the market share of power plants flue gas desulfurization more than 90%.At present, the desulfuration efficiency of existing wet desulfurization of flue gas by limestone-gypsum method technique can reach more than 95% usually.
The guiding of national policy, impels coal steam-electric plant smoke pollutant to draw close towards ultra-clean or near-zero release level.Flue gas pollutant discharge will meet: particle (PM) < 5.0mg/Nm
3, SO
2< 20mg/Nm
3, NO
x< 30mg/Nm
3.When sulfur dioxide in flue gas concentration is greater than 2000mg/Nm
3time, meet sulfur dioxide concentration and reach ultra-clean or near-zero release level, desulfuration efficiency must be greater than the desulfuration efficiency of 99% or higher, existing wet desulfurization of flue gas by limestone-gypsum method technique will be difficult to reach so high desulfuration efficiency, its common improving one's methods is the spray number of plies increasing absorption tower, spraying layer as arranged more than 5 layers strengthens the mode of spray flux to improve desulfuration efficiency, but the mode that this simple increase spraying layer strengthens spray flux will corresponding increase circulation pump power, causes the significantly increase running power consumption and cost.
In addition, current wet desulfurization of flue gas by limestone-gypsum method technique is the drop of neat stress band high concentration limestone/gypsum solid particle after ubiquity gypsum rain phenomenon or desulfurization also, drop solid content reaches 15-30% usually, add difficulty to the subsequent treatment of desulfurization downstream PM, be difficult to ensure PM < 5.0mg/Nm
3index request.
Utility model content
The purpose of this utility model is: propose a kind of operation energy consumption is low, can realize the ultra-clean discharge of flue gas sulfur method and device, solves existing wet desulfurization of flue gas by limestone-gypsum method technique desulfurization neat stress and carries the drop of high solid concentration, desulfuration efficiency is low, desulfurizing byproduct gypsum qualitt is not high and operation energy consumption is high problem.
The utility model object is realized by following technical proposals:
A kind of low energy consumption, the flue gas desulfur device of ultra-clean discharge, comprise absorption plant, it has the smoke inlet of bottom, with the spray equipment on top, and the slurry pool of bottom, described spray equipment comprises some spraying layers, it is characterized in that: also comprise slurry tank, and described spraying layer is separated into the secondary slurries spraying layer of top and the one-level slurries spraying layer of below, form the gas-liquid part flow arrangement of two independent serum recycle systems, wherein one-level serum recycle system comprises the described one-level slurries spraying layer be connected, and collect desulfurization slurry of its spray below it and return the described slurry pool of described one-level slurries spraying layer, secondary serum recycle system comprises described secondary slurries spraying layer, the described gas-liquid part flow arrangement of the desulfurization slurry of its spray is collected below it, and collect the desulfurization slurry of described gas-liquid part flow arrangement and return the slurry tank of described secondary slurries spraying layer.
In such scheme, flue gas flows from bottom to top at desulfurizer, the slurries counter current contacting first sprayed with the one-level slurries spraying layer in one-level serum recycle system, the SO in flue gas
2a primary wash generation Dry FGD is carried out with desulfurizer slurry; Flue gas continues upwards to flow, and with the slurries counter current contacting that sprays in the secondary slurries spraying layer in secondary serum recycle system, the SO in flue gas
2generation desulphurization reaction is again washed with desulfurizer slurry.
Meanwhile, adopt the program, can hinge structure adopt the spray number of plies of less number of plies just can realize the effect of prior art, meet higher environmental requirement with lower energy consumption.
This programme adopts gas-liquid part flow arrangement absorption tower spraying layer to be separated into two independently desulfurization sprayed slurry circulatory systems, adopts the three-circulation desulphurization of two slurry pool/case, two serum density, control zones of different slurry pH value, reaches reduction energy consumption, meets PM, SO
2ultra-clean or near-zero release object.By two independently desulfurization sprayed slurry circulatory systems, two slurry pool/case is set, realize controlling the different serum density of two slurry pool/case, realize the pH value controlling zones of different slurries, the object that after realizing desulfurization, neat stress drop solid content is greater than 99% lower than 10% and system desulfuration efficiency simultaneously.
As selection, described gas-liquid part flow arrangement comprises diversion mechanism and collecting mechanism, described collecting mechanism collects after described secondary slurries spraying layer sprays the desulfurization slurry wandered to diversion mechanism and is delivered to described slurry tank, and the slurries liquid film that between diversion mechanism and collecting mechanism, gap-forming can be passed through for flue gas.
In such scheme, flue gas passes from bottom to top from the slurries liquid film that Gong the flue gas formed between the diversion mechanism and collecting mechanism of gas-liquid part flow arrangement passes through, and flue gas contacts with slurries liquid film and carries out secondary washing generation Dry FGD in the process.
As further selection, described gas-liquid part flow arrangement is ridge type gas-liquid part flow arrangement, comprise shunting ridge, and collecting tank below it and collecting tray, shunting ridge and collecting tank are with the positive and negative mirror image interlaced arrangement of ridge pattern, collecting tank collects the slurries that shunting ridge is wandered, and collecting tray collects the slurries of described collecting tank and is delivered to described slurry tank.
In such scheme, ridge type gas-liquid part flow arrangement has flue gas/slurry diversion function, has desulfurizing function simultaneously.Absorption plant desulfurization comprises three washing flue gas desulfurizations above a primary wash flue gas desulfurization below ridge type part flow arrangement, the secondary washing flue gas desulfurization of ridge type part flow arrangement and ridge part flow arrangement, and ridge type gas-liquid part flow arrangement sweetening process can make system desulfuration efficiency improve 10-50%.
As further selecting, described collecting tank and collecting tray tilt to serum outlet direction, and angle of inclination is and horizontal direction angle 3-15 °.
In such scheme, collecting tank and collecting tray tilt to serum outlet direction, deposit in collecting tank and collecting tray to prevent the solid in desulfurization slurry.
As selection, also comprise desulfurization slurry replenishment system, described desulfurization slurry replenishment system respectively with slurry pool to the pipeline of one-level slurries spraying layer, and slurry tank is to the pipeline connection of secondary slurries spraying layer.
In such scheme, desulfurization slurry replenishment system respectively with slurry pool to the pipeline of one-level slurries spraying layer, and slurry tank is to the pipeline connection of secondary slurries spraying layer, fresh slurry is directly added in system spray, having abandoned in prior art is all the mode adding slurries in slurry pool/slurry tank, improve the pH of sprayed slurry, be beneficial to slurries to flue gas SO
2absorption, improve desulfuration efficiency, and in cyclic process, slurries absorb flue gas SO
2after again gravity drop into slurry pool/slurry tank, due to desulfurization chemical reaction effect, slurry pH value reduces again naturally, is beneficial to oxidation and the crystallization of desulfurizing byproduct gypsum, improve gypsum qualitt, kill two birds with one stone.
As selection, described slurry tank gravity flow is communicated to described slurry pool, and described slurry pool is provided with desulfurizing byproduct discharger.
In such scheme, slurry tank gravity flow is communicated to slurry pool, can be discharged to the slurries amount of slurry pool, can reduce the serum density of secondary serum recycle simply and effectively by controlling slurry tank, to meet drop solid content that desulfurization neat stress carries lower than 10%, be beneficial to desulfuration efficiency simultaneously and improve; Slurry tank enters slurry pool on the one hand, and slurry pool is provided with desulfurizing byproduct discharger on the other hand, the simple serum density effectively improving one-level serum recycle system, for the gypsum treatment in downstream creates conditions, improves gypsum purity, kills two birds with one stone; Slurry tank is carried out high liquid level layout simultaneously, realize gravity flow and discharge, fraction slurries circulation pump lift can be reduced again, thus the power configuration of reduction fraction slurries circulating pump is to reduce desulfurization operation power consumption, killing three birds with one stone.
As selection, one-level/secondary slurries spraying layer number of plies is respectively 2 layers.
In such scheme, only needing 4 layers just can realize prior art needs more than the 5 layers desulfuration efficiencies that could realize to reach more than 99%; Under more multi-layered said conditions, slurries 100% ground that can also realize being difficult in prior art realize absorbs flue gas SO
2, thus realize zero-emission truly.
As selection, also comprise three grades of serum recycle systems, it comprises the described slurry pool, the three grades of slurry circulating pumps that are communicated with successively and form circulation, and is located at three grades of slurries jetted layers in described slurry pool.
In such scheme, three grades of serum recycle systems, realize slurry pool slurries Homogeneous phase mixing, object that oxidation air is evenly sent out, thus improve desulfurizing byproduct gypsum qualitt and prevent desulfurizing byproduct from causing fouling, blocking at slurry pool bottom precipitation.
As selection, also comprise oxidation air system, it comprises the oxidation fan of connection, and is located at the oxidation air pipe of described slurry pool and slurry tank.
In such scheme, promote gypsum oxidation by air oxidation, be conducive to pH value simultaneously further and control in lower scope, be more conducive to gypsum oxidation, crystallization, improve gypsum qualitt.
As selection, described slurry pool is connected with the pump that falls mutually also arranged between slurry tank in order to slurries are emptying.
In such scheme, slurries emptying mutual pump is set between slurry pool and slurry tank, without the need to arranging separately the emptying accident slurry tank of slurries again, cost of reducing investment outlay.
The main scheme of aforementioned the utility model and each further selection scheme thereof can independent assortment to form multiple scheme; be the utility model can adopt and claimed scheme: as the utility model; each selection can select any combination with other; those skilled in the art can understand there is multiple combination according to prior art and common practise after understanding the utility model scheme; be the claimed technical scheme of the utility model, do not do exhaustive at this.
The beneficial effects of the utility model: the utility model provides the desulfurizer that a kind of operation energy consumption is low, can realize the ultra-clean discharge of flue gas.Desulfurization slurry is separated into two independently desulfurization sprayed slurry circulatory systems by the utility model, adopt the three-circulation desulphurization of two slurries gathering-device (slurry pool/case), two serum density, control zones of different slurry pH value, reach reduction energy consumption, meet PM, SO
2ultra-clean or near-zero release object.By the pH value arranging two slurry pool/case, control the different serum density of two slurry pool/case, control zones of different slurries, and form two independently serum recycle loops, the object that after realizing desulfurization, neat stress drop solid content is greater than 99% lower than 10% and system desulfuration efficiency; Arranged by the outer slurry tank high liquid level of tower, and less spraying layer, reach and reduce circulation pump power, reduction desulfurization operation power consumption object; By arranging three grades of serum recycle systems in slurry pool of absorption tower, coordinating oxidation air system, making the full and uniform mixing of slurries in slurry pool, reach complete oxidation desulfurizing byproduct, improve gypsum qualitt and purity and reach more than 95% and prevent the object of slurry deposition.
Accompanying drawing explanation
Fig. 1 is the device schematic flow sheet of the utility model embodiment.
Detailed description of the invention
Following non-limiting examples is for illustration of the utility model.
A flue gas desulfur device for low energy consumption, ultra-clean discharge, shown in figure 1:
1, flue gas line:
Between the spraying layer of absorption tower 1, arrange ridge type gas-liquid part flow arrangement 6-5, ridge type gas-liquid part flow arrangement 6-5 forms by shunting ridge 6-51, collecting tank 6-52 and collecting tray 6-53, and ridge 6-51 and collecting tank 6-52 is with the positive and negative mirror image interlaced arrangement of ridge pattern in shunting.6-51 is horizontally disposed for shunting ridge, and collecting tank 6-52 and collecting tray 6-53 tilts to serum outlet direction, and to prevent the solid in desulfurization slurry from depositing in collecting tank and collecting tray, angle of inclination is and horizontal direction angle 3-15 °.The slurries of spray form liquid film between shunting ridge 6-51 and collecting tank 6-52.
Flue gas flows from bottom to top after the smoke inlet 2 on absorption tower 1 enters absorption tower 1, the slurries counter current contacting first sprayed with the one-level slurries spraying layer 5-4 in one-level serum recycle spray system 5, the SO in flue gas
2a primary wash generation Dry FGD is carried out with desulfurizer slurry; Flue gas passes from bottom to top from the gap between the shunting ridge 6-51 and collecting tank 6-52 of ridge type gas-liquid part flow arrangement 6-5 subsequently, flue gas and contact carry out secondary washing generation Dry FGD along shunt slurries liquid film that ridge 6-51 edge flows down in the process, this process can make system desulfuration efficiency raising 10-50%; Flue gas is through continuing upwards to flow after ridge type gas-liquid part flow arrangement, and the slurries counter current contacting sprayed with the secondary slurries spraying layer 6-4 in secondary serum recycle system 6, the SO in flue gas
2carry out washing for three times with desulfurizer slurry and desulphurization reaction occurs; Flue gas will flow through the demister 7 being arranged on top, absorption tower 1 after passing completely through slurries spraying layer 6-4, and after the most of droplet in flue gas is removed, after desulfurization, neat stress discharges absorption tower 1 by exhanst gas outlet 3, and the drop solid content in neat stress is lower than 10%.After the serous adverse flow washing of the high ph-values of three 5.5-8.5 in two-stage serum recycle system, system desulfuration efficiency can reach more than 99%, and even slurries 100% ground absorbs flue gas SO
2.
2, slurry line:
1) desulfurizer slurry that a part is fresh is connected with the one-level serum recycle carrier pipe 5-3 before one-level serum recycle system spraying layer 5-4 entrance by pipeline 5-5.The slurries that fresh desulfurizer slurry and one-level slurry circulating pump 5-2 pump deliver to one-level slurries spraying layer 5-4 by one-level serum recycle conveyance conduit 5-3; The slurries that slurries spraying layer 5-4 sprays pH value 5.5-8.5 are conducive to slurries to flue gas SO
2absorption, improve desulfurization performance.SO from the desulfurizer slurry and flue gas of slurries spraying layer 5-4 ejection
2drop into slurry pool of absorption tower 4 after there is desulphurization reaction, form one-level serum recycle.Fresh desulfurizer slurry by pipeline 5-5 also can with before one-level serum recycle delivery pump 5-2, the primary cycle serum outlet pipe 5-1 of slurry pool of absorption tower 4 is connected.Desulfurizing byproduct gypsum in the slurry pool of absorption tower 4 of one-level serum recycle system delivers to the gypsum rotational flow station process in downstream through gypsum excavationg pump 11.By gypsum excavationg pump 11, the serum density controlling one-level serum recycle system is 1150-1300kg/m
3, for the gypsum treatment in downstream creates conditions, improves gypsum purity.
2) another part fresh slurry is connected with the secondary serum recycle carrier pipe 6-3 before secondary serum recycle system spraying layer 6-4 entrance by pipeline 6-8, and the slurries that fresh desulfurizer slurry and secondary slurry circulating pump 6-2 pump deliver to secondary slurries spraying layer 6-4 by secondary serum recycle conveyance conduit 6-3; The slurries that slurries spraying layer 6-4 sprays pH value 5.5-8.5 are conducive to slurries to flue gas SO
2absorption, improve desulfurization performance.From slurries spraying layer the 6-4 desulfurizer slurry sprayed and the SO passed the flue gas of ridge type gas-liquid part flow arrangement 6-5
2after carrying out three washing generation desulphurization reactions, collected by ridge type gas-liquid part flow arrangement 6-5, and get back to tower outer slurry tank 8 from the secondary cycle injection point 6-7 of slurry tank tower 8 with flow by gravity form through slurries introduction pipe 6-6, form secondary serum recycle.Fresh desulfurizer slurry also can with before secondary serum recycle delivery pump 6-2, outside tower, the secondary cycle serum outlet pipe 6-1 of slurry tank 8 be connected by pipeline 6-8.The outer slurry tank 8 of tower is provided with agitating device 8-1 or other prevent the device of slurry deposition, precipitates in the outer slurry tank 8 of tower to prevent desulfurizing byproduct.
One-level/secondary serum recycle system spraying layer sprayed slurry/uptake zone slurry pH value brings up to 6.0-6.5 from 5.0-5.5, and desulfuration efficiency can improve 3-5%.
3) a liquid level high position for the outer slurry tank 8 of the tower of secondary serum recycle system designs or is arranged on the support of certain altitude by outer for tower slurry tank 8, reduce the circulation pump lift of secondary slurries system, reach and reduce circulation pump power, significantly reduction desulfurization operation power consumption object.As for 1 600MW generator set desulfurization, when desulfuration efficiency 98.4% designs, the circulating pump power consumption of the utility model technique saves power consumption 1500kW.h/h than common process.
4) the outer slurries of slurry tank 8 of the tower of secondary serum recycle system and the liquid level of slurry pool of absorption tower 4 have certain difference in height.Tower outer slurry tank 8 desulfurization product outlet 8-2 can flow into slurry pool of absorption tower 4 by gravity through desulfurizing byproduct conveyance conduit 13, desulfurizing byproduct conveyance conduit 13 can arrange its flow of valve regulated, or to adopt other modes to control secondary serum recycle system slurry density be 1150kg/m
3below, make secondary serum recycle system slurry be that low-density medium runs, can control below 10% by the neat stress drop solid content after desulfurization, for the removal of desulfurization downstream fume gas PM creates conditions, slurry medium density is from 1150-1300kg/m simultaneously
3be reduced to 1150kg/m
3below, can promote that slurries are to flue gas SO
2absorption, improve desulfuration efficiency 1-3%.
5) slurry pool slurries in tower are extracted out from upper slurry outlet 9-1 and are applied to return in tower after energy through three grades of slurry circulating pump 9-2 again by three grades of serum recycle systems 9, slurries are ejected into bottom slurry pool 4 through three grades of slurries jetted layers 9-3, make slurries Homogeneous phase mixing in tower and keep suspended state, preventing desulfurizing byproduct from causing fouling, blocking at slurry pool 4 bottom precipitation.In absorption tower, slurry pool slurries also can adopt mechanical agitation to realize slurries suspension and prevent slurry deposition.
6) one-level/secondary serum recycle system slurry all arranges oxidation air system, and oxidation air system is made up of the outer slurry tank oxidation air pipe 10-4 of oxidation fan 10-1, common conduit 10-2, one-level serum recycle Systemic absorption tower stock tank oxidation air pipe 10-3 and secondary serum recycle system tower.Slurry pool of absorption tower slurries and the outer slurry tank slurry pH value of tower control within the scope of 4.0-5.5, are conducive to gypsum oxidation, crystallization, improve gypsum qualitt.
7) the outer slurry tank 8 of tower and the double accident slurry tank doing desulphurization system of slurry pool of absorption tower 4, tower is outer to be connected by pipeline between slurry tank 8 and slurry pool of absorption tower 4, arrange slurries falls pump 12 mutually, break down when the outer slurry tank 8 of absorption tower 1 and tower need maintenance time, the slurries realizing two case ponds fall mutually, saving accident slurry tank cost.
8) one-level/secondary serum recycle system spray number of plies is respectively layer 2-4.
9) fresh desulfurization slurry is lime stone slurry or lime slurry or other forms of slurries etc.
The fume desulphurization method of aforementioned means, the flue gas comprised from bottom to top is washed by top-down spray equipment spray desulfurization slurry counter current contacting, described desulfurization slurry forms independently two-stage serum recycle, wherein one-level serum recycle comprises one-level spray equipment, and collect desulfurization slurry of its spray below it and return the one-level slurries gathering-device of described one-level spray equipment, described flue gas carries out once washing in described one-level serum recycle, secondary serum recycle comprises the secondary spray equipment be positioned at above one-level spray equipment, and collect desulfurization slurry of its spray below it and return the secondary slurries gathering-device of described secondary spray equipment, described flue gas again washs in described secondary serum recycle, described one, the desulfurization slurry pH value of secondary spray equipment spray controls at 5.5-8.5, one, desulfurization slurry pH in secondary slurries gathering-device controls at 4.0-5.5, in described secondary serum recycle, the serum density of desulfurization slurry controls at 1150kg/m
3below, the serum density of the desulfurization slurry in one-level serum recycle controls at 1150-1300kg/m
3.
In such scheme, break prior art desulfurization slurry simple subprogram scheme for a long time, ingehious design is two-stage serum recycle independently, realize different pH and serum density thus to control simultaneously, finally realize simultaneously low energy consumption, low PM, high desulfurization efficiency, high gypsum qualitt one action four effect:
Different by the pH value of controlled circulation system zones of different slurries, reach simultaneously and improve desulfuration efficiency and be beneficial to desulfurizing byproduct (gypsum) oxidation and crystallization object, namely the pH value improving spray equipment sprayed slurry/uptake zone slurries reaches 5.5-8.5, is beneficial to slurries to flue gas SO
2absorption, improve desulfuration efficiency, and in cyclic process, slurries absorb flue gas SO
2after again gravity drop into I and II slurries gathering-device, due to desulfurization chemical reaction effect, slurry pH value is reduced to 4.0-5.5, is beneficial to oxidation and the crystallization of desulfurizing byproduct gypsum, improve gypsum qualitt, kill two birds with one stone.
By two-stage independent loops, make two independent serum recycle systems have different serum densities, realize respective favourable function, namely one-level serum recycle serum density controls as 1150-1300kg/m
3, be beneficial to the desulfurizing byproduct that desulfurizer arranges outward and carry out dewatering, improving gypsum purity; Secondary serum recycle serum density controls as 1150kg/m
3below, to meet drop solid content that desulfurization neat stress carries lower than 10%, be beneficial to desulfuration efficiency simultaneously and improve, again realize killing two birds with one stone object.
On aforementioned base, in one-level serum recycle, the slurries counter current contacting that first flue gas sprays with the one-level slurries spray equipment in one-level serum recycle, the SO in flue gas
2a primary wash generation Dry FGD is carried out with desulfurizer slurry; In secondary serum recycle, the slurries counter current contacting that flue gas sprays with the secondary slurries spray equipment in secondary serum recycle again, the SO in flue gas
2generation desulphurization reaction is again washed with desulfurizer slurry; The slurries of the high ph-values of 5.5-8.5 repeatedly in two-stage serum recycle system, and 1150kg/m in secondary cycle
3after following low serum density serous adverse flow washing, system desulfuration efficiency can reach more than 99%.
Simultaneously, adopt the program, can hinge structure adopt the spray number of plies of less number of plies just can realize the effect of prior art, meet higher environmental requirement with lower energy consumption, the desulfurization neat stress drop solid content realizing contributing to downstream PM process lower than 10%, SO
2concentration of emission meets ultra-clean or near-zero release level or desulfuration efficiency is greater than 99%, realize desulfurizing byproduct oxidation completely, the gypsum purity object that is greater than 95%.
As selection, form the slurries liquid film that can pass through for flue gas between described secondary spray equipment and secondary slurries gathering-device, flue gas is again washed in by the process of liquid film.
In such scheme, flue gas flows from bottom to top at desulfurizer, the slurries counter current contacting first sprayed with the one-level slurries spray equipment in one-level serum recycle, the SO in flue gas
2a primary wash generation Dry FGD is carried out with desulfurizer slurry; Flue gas passes from bottom to top from the slurries liquid film that Gong the flue gas formed between secondary spray equipment and secondary slurries gathering-device passes through subsequently, flue gas contacts with slurries liquid film and carries out secondary washing generation Dry FGD in the process, and this process can make system desulfuration efficiency improve 10-50%; Flue gas continues upwards to flow, and with the slurries counter current contacting that sprays in the secondary slurries spray equipment in secondary serum recycle, the SO in flue gas
2carry out washing for three times with desulfurizer slurry and desulphurization reaction occurs.The slurries of the high ph-values of three 5.5-8.5 in two-stage serum recycle system, twice 1150kg/m in secondary cycle
3after following low serum density serous adverse flow washing, slurries 100% ground that system desulfuration efficiency can realize being difficult in prior art realize absorbs flue gas SO
2, thus realize zero-emission truly.
As selection, described one-level slurries gathering-device also carries out slurries inner loop.
In such scheme, hinge structure adopts churned mechanically mode usually, mechanical agitation is subject to the restriction of sphere of action, it is bad that oxidation air sends out effect, exist and stir dead angle, cause that desulfurizing byproduct is oxidized not exclusively, gypsum qualitt is not high thus, occur that desulfurizing byproduct precipitates bottom slurry pool, and cause the phenomenons such as slurry pool fouling, line clogging.The utility model scheme, by slurries inner loop, makes slurries Homogeneous phase mixing in tower and keeps suspended state, improves desulfurizing byproduct gypsum qualitt and prevents desulfurizing byproduct from causing fouling, blocking at slurry pool bottom precipitation.
As selection, described I and II slurries gathering-device is communicated with and can the mutual emptying desulfurization slurry of pumping.
In such scheme, can be discharged to the slurries amount of one-level serum recycle by controlling secondary serum recycle, the serum density controlling secondary serum recycle is simply and effectively 1150kg/m
3below; Meanwhile, can pump be emptying mutually, thus without the need to arranging separately the emptying accident slurry tank of slurries again, cost of reducing investment outlay between the one-level slurries gathering-device of one-level serum recycle and the secondary slurries gathering-device of secondary serum recycle.As previously mentioned, kill two birds with one stone.
As selection, described I and II slurries gathering-device all passes into air and is oxidized.
In such scheme, promote gypsum oxidation by air oxidation, be conducive to pH value further simultaneously and control within the scope of 4.0-5.5, be more conducive to gypsum oxidation, crystallization, improve gypsum qualitt.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. a low energy consumption, the flue gas desulfur device of ultra-clean discharge, comprise absorption plant, it has the smoke inlet of bottom, with the spray equipment on top, and the slurry pool of bottom, described spray equipment comprises some spraying layers, it is characterized in that: also comprise slurry tank, and described spraying layer is separated into the secondary slurries spraying layer of top and the one-level slurries spraying layer of below, form the gas-liquid part flow arrangement of two independent serum recycle systems, wherein one-level serum recycle system comprises the described one-level slurries spraying layer be connected, and collect desulfurization slurry of its spray below it and return the described slurry pool of described one-level slurries spraying layer, secondary serum recycle system comprises described secondary slurries spraying layer, the described gas-liquid part flow arrangement of the desulfurization slurry of its spray is collected below it, and collect the desulfurization slurry of described gas-liquid part flow arrangement and return the slurry tank of described secondary slurries spraying layer.
2. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, it is characterized in that: described gas-liquid part flow arrangement comprises diversion mechanism and collecting mechanism, described collecting mechanism collects after described secondary slurries spraying layer sprays the desulfurization slurry wandered to diversion mechanism and is delivered to described slurry tank, and the slurries liquid film that between diversion mechanism and collecting mechanism, gap-forming can be passed through for flue gas.
3. the flue gas desulfur device of low energy consumption as claimed in claim 2, ultra-clean discharge, it is characterized in that: described gas-liquid part flow arrangement is ridge type gas-liquid part flow arrangement, comprise shunting ridge, and collecting tank below it and collecting tray, shunting ridge and collecting tank are with the positive and negative mirror image interlaced arrangement of ridge pattern, collecting tank collects the slurries that shunting ridge is wandered, and collecting tray collects the slurries of described collecting tank and is delivered to described slurry tank.
4. the flue gas desulfur device of low energy consumption as claimed in claim 3, ultra-clean discharge, is characterized in that: described collecting tank and collecting tray tilt to serum outlet direction, and angle of inclination is and horizontal direction angle 3-15 °.
5. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, it is characterized in that: also comprise desulfurization slurry replenishment system, described desulfurization slurry replenishment system respectively with slurry pool to the pipeline of one-level slurries spraying layer, and slurry tank is to the pipeline connection of secondary slurries spraying layer.
6. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, is characterized in that: described slurry tank gravity flow is communicated to described slurry pool, and described slurry pool is provided with desulfurizing byproduct discharger.
7. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, it is characterized in that: also comprise three grades of serum recycle systems, it comprises the described slurry pool, the three grades of slurry circulating pumps that are communicated with successively and form circulation, and is located at three grades of slurries jetted layers in described slurry pool.
8. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, it is characterized in that: also comprise oxidation air system, it comprises the oxidation fan of connection, and is located at the oxidation air pipe network of described slurry pool and slurry tank.
9. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, is characterized in that: described slurry pool is connected with the pump that falls mutually also arranged between slurry tank in order to slurries are emptying.
10. the flue gas desulfur device of low energy consumption as claimed in claim 1, ultra-clean discharge, is characterized in that: described one-level/secondary slurries spraying layer number of plies is respectively 2 layers.
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| CN201420553295.0U CN204121971U (en) | 2014-09-23 | 2014-09-23 | The flue gas desulfur device of a kind of low energy consumption, ultra-clean discharge |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109316942A (en) * | 2018-10-17 | 2019-02-12 | 山东国舜建设集团有限公司 | It is a kind of to connect liquid device for single column double-cycle process scrubbing tower |
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2014
- 2014-09-23 CN CN201420553295.0U patent/CN204121971U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109316942A (en) * | 2018-10-17 | 2019-02-12 | 山东国舜建设集团有限公司 | It is a kind of to connect liquid device for single column double-cycle process scrubbing tower |
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