CN201179413Y - Column top discharge type flue gas desulfurization column equipped with material filling segment - Google Patents
Column top discharge type flue gas desulfurization column equipped with material filling segment Download PDFInfo
- Publication number
- CN201179413Y CN201179413Y CNU2008200554835U CN200820055483U CN201179413Y CN 201179413 Y CN201179413 Y CN 201179413Y CN U2008200554835 U CNU2008200554835 U CN U2008200554835U CN 200820055483 U CN200820055483 U CN 200820055483U CN 201179413 Y CN201179413 Y CN 201179413Y
- Authority
- CN
- China
- Prior art keywords
- smoke
- desulfurizing tower
- tower
- nozzle
- tower body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims description 38
- 239000003546 flue gas Substances 0.000 title claims description 38
- 238000006477 desulfuration reaction Methods 0.000 title claims description 17
- 230000023556 desulfurization Effects 0.000 title claims description 17
- 239000000463 material Substances 0.000 title description 6
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims description 31
- 238000012856 packing Methods 0.000 claims description 28
- 239000007921 spray Substances 0.000 claims description 26
- 239000003517 fume Substances 0.000 claims description 12
- 238000013459 approach Methods 0.000 claims description 10
- 239000000945 filler Substances 0.000 claims description 10
- 239000013505 freshwater Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000004033 plastic Substances 0.000 claims description 5
- 229920003023 plastic Polymers 0.000 claims description 5
- 229920000114 Corrugated plastic Polymers 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 239000000779 smoke Substances 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 13
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 6
- 238000013461 design Methods 0.000 abstract description 3
- 239000008258 liquid foam Substances 0.000 abstract description 3
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 abstract description 3
- 239000013530 defoamer Substances 0.000 abstract 2
- 239000007788 liquid Substances 0.000 description 15
- 238000010521 absorption reaction Methods 0.000 description 14
- 230000005587 bubbling Effects 0.000 description 12
- 239000002253 acid Substances 0.000 description 8
- 238000005260 corrosion Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 230000002708 enhancing effect Effects 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000001095 magnesium carbonate Substances 0.000 description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 2
- 235000019341 magnesium sulphate Nutrition 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a tower top exhaustion type smoke desulfurizing tower with a filling section. The smoke desulfurizing tower comprises a tower body, a smoke inlet and a smoke outlet which are arranged on the tower body, and an upright chimney arranged above the smoke outlet. After the smoke is desulfurized and purified in the desulfurizing tower body, especially after the oxysulfide in the smoke is recovered for producing sulfate products, the smoke can be directly exhausted from the upright chimney. The smoke desulfurizing tower is innovatively characterized in that the inside of the tower body is provided with the filling section which is used for removing liquid foams carried in the smoke with high efficiency so as to ensure the exhaustion index of the smoke purification and particularly protects the upright chimney from forming scale, namely, the filling section is also a defoamer. The design has the advantage that the defoamer is coupled in the tower top exhaustion type smoke desulfurizing tower, thereby simplifying the technical process, saving the occupation area and the investment.
Description
Technical field
The utility model relates to a kind of tower top discharge type flue gas desulfurization emission abatement integration apparatus that is provided with packing section, relate in particular to and from flue gas, reclaim the desulfurizing tower that oxysulfide is produced useful products, belong to electric power, metallurgy, environmental protection and chemical technology field, especially be fit to the flue gas desulfurization technique field.
Background technology
With coal or oil is that a large amount of boiler flues are discharged in the thermal power plant of fuel, directly arranges to atmosphere through chimney.The blowdown stack height of boiler of power plant generally all adopts reinforcing bar to mix earth material as the intensity shell between 120～250m.Owing to contain acidic gaseous materials such as SOx, NOx, HCl and HF, SO especially wherein in the flue gas
3Gas makes flue gas show acid dew piont corrosion.The acid dew point of flue gas is with SO in the flue gas
3Increase and increase with moisture content, generally between 100～150 ℃.In order to ensure not occurring acid dew piont corrosion in the fume emission process, from the steam generator system outlet, the flue-gas temperature of promptly common boiler induced-draft fan outlet is higher 15～25 ℃ than dew point.But for the purpose of safety and over-designed, inner wall of stack all needs liner insulation, especially anti-corrosion material, and with acid resistant adhesive mortar, inferior nexine lining is with acidproof brick at the innermost layer lining that contacts with flue gas.
Along with environmental requirement is more and more stricter, power plant or boiler all need to install flue gas desulfur device, and the flue gas desulfurization technique of main flow all is the method that the aqueous slurry washing absorbs, or be called wet method, desulfurizing agent is an alkaline matter, such as natural lime stone, i.e. calcium carbonate, magnesia/magnesium carbonate, NaOH/sodium carbonate, perhaps synthetic ammonia etc., desulfurization product is respectively gypsum (a calcium sulphate dihydrate crystal), epsom salt crystal, sodium sulphate or ammonium sulfate.A common ground of these methods all is that the desulfidation tail gas exhaust temperature is lower than the acid dew piont corrosion temperature, and near the water saturated water dew point temperature of flue gas, between 40～60 ℃, although at desulphurization plant, is commonly referred in the desulfurizing tower SO
3Removal efficiency also very high, but because SO
3Meet water and can form acid mist, impossible 100% removes, and the tail gas after the desulfurization contains sulfuric acid mist, still shows obvious corrosion.
Existing method is that the original chimney of boiler is further implemented anti-corrosion treatment, such as at original acid resistant adhesive mortar layer inside lining anti-corrosive material again, strengthens its anti-corrosion capability.For newly-built unit, the anticorrosion construction period that makes of enhancing property prolongs greatly, and the anticorrosion chimney construction cost that makes of enhancing property increases, and the difficulty that follow-up maintenance and anti-corrosion material upgrade is also very big.For old unit, if original chimney is carried out new preservative treatment, difficulty of construction is big, long construction period, and more crucial is that this production to unit or boiler can affect greatly, and lacks using value in practice.
Summary of the invention
The utility model technical issues that need to address are to disclose a kind of novel tower top discharge type flue gas desulfurization discharging integration apparatus that is provided with packing section, especially disclose a kind of desulfurizing tower that reclaims oxysulfide from flue gas.It gas cleaning after, directly the upright chimney discharging that connects from the exhanst gas outlet of desulfurizing tower does not need again through original smoke stack emission flue gas.Therefore, the upright chimney that the utility model is mentioned, perhaps in line chimney, perhaps in line chimney, perhaps in line flue is exactly the exhanst gas outlet that directly is connected fume desulfurizing tower, direct member to airborne release tail gas.The desulfurizing tower that this member is installed is emission purification gas directly.Like this, chimney originally no longer needs to carry out anticorrosion enhancing to be handled, even original chimney discarded fully, overcome the above-mentioned defective that prior art exists, and its energy consumption is low, the purification efficiency height.
Essence of the present utility model also is; be provided with packing section in desulfurizing tower inside; in order to the liquid foam of being carried secretly in the flue gas of efficient removal through absorption liquid spray washing and absorption cleaning; to guarantee to purify the discharge index of flue gas; especially protect non-scaling in the upright chimney that discharges flue gas, therefore, the major function of this packing section is foam removal; or demist, also can be described as demister or demister.The advantage of this design is that coupling is provided with demister in tower top discharge type desulfurization tower body, has simplified technological process, makes equipment more compact, has saved floor space, also can reduce investment outlay.
Particularly, the disclosed fume desulfurizing tower of the utility model is meant as having the tower top discharge type flue gas desulfurization tower of packing section, is cylindrical shape or square tower, and its novelty design also comprises:
Tower body;
Gas approach on the tower body, position between tower body middle and lower part or middle and lower part to middle and upper part, preferred middle part;
Exhanst gas outlet on the tower body, the position is in tower body top or top, preferred top;
Be arranged on the packing section in the tower body between gas approach and the exhanst gas outlet;
Be arranged on the spray section in the tower body between gas approach and the packing section;
Be arranged on the bubbling segment that is positioned at tower body of gas approach bottom;
Be arranged on and purify on the exhanst gas outlet, and the upright chimney that directly is connected with exhanst gas outlet; And,
The flow area of the gas approach on the described tower body is a rectangle, and is perhaps approximate rectangular, and the ratio on the minor face of described rectangle and long limit is between 0.25-0.5;
Be provided with flue gas distributor in the spray section, absorption liquid spray thrower and liquid wall stream baffle plate;
Be provided with air bubbler and side in the bubbling segment and advance an agitator;
The cross section of upright chimney be circular, ellipse, square, perhaps rectangle,
The cross-sectional area of upright chimney is 0.10～0.25 times of tower body cross-sectional area, preferably between 0.125～0.175m;
The height of upright chimney is between 20～100m, preferably between 30～70m;
Its inventive features also is,
Described packing section comprises two-layer filler, the below of packing layer or below are provided with fresh water (FW) rinse spray device, spray thrower comprises distributor pipe and nozzle, distributor pipe is connected with nozzle, distributor pipe is divided into to be responsible for and arm, the person in charge is connected with arm, and the person in charge's internal diameter is 0.1～0.3m, and the internal diameter of arm is 0.05～0.15mm;
Described nozzle quantity is, on the cross section of described tower body, arranges 1 nozzle for per 0.5～2.0 square metre, and the spout internal diameter of nozzle is 5～20mm, is preferably 7～12mm;
Described packing layer uses the corrugated plastic plate to be arranged in parallel and forms, sheet spacing 10～50mm is preferably 20～35mm, and the thickness of described plate is 1.0mm～5.0mm, preferred 2.0mm～3.5mm, and described plastic plate adopts the plastic production of glass fibre enhancing.
The disclosed smoke eliminator of the utility model is operated in the following manner:
Contain SO
2(content is generally at 500-15000mg/Nm
3), SO
3(content is generally at 10-300mg/Nm
3), (content is generally at 100-1000mg/Nm for NOx
3), (content is generally at 10-100mg/Nm for HCl/HF
3), (content is generally at 50-500mg/Nm for dirt
3) wait pollutant, and temperature is 100-160 ℃ flue gas, enters desulfurizing tower from gas approach, the spray section of upwards flowing through, with spray the washing absorption liquid counter current contacting of getting off from spray thrower, the chemical reaction in mass transfer, heat transfer and the liquid phase of solution-air two-phase takes place, deviate from above pollutant.In spray section, the SO in the flue gas
2Become sulphite, SO
3Become sulfate, HCl becomes chloride.The eliminating efficiency of these highly acid pollutants can reach 95%.The eliminating efficiency of the flyash in the flue gas (dirt) is greater than 60%-90%.Flue gas is washed the absorption liquid cold shock, and temperature is reduced to 40-60 ℃.
The washing absorption liquid is the pulpous state aqueous solution that contains alkaline desulfurizing agent, sulfate and crystalline solid thereof, and general saturated or oversaturated pulpous state aqueous mixtures by sulfate all.
Big for unit or boiler capacity, perhaps SO in the flue gas
2The situation that concentration is high, if adopt extremely low calcium raw material (calcium method) or the magnesium raw material (magnesium method) of solubility, the cleaning solution flow will be very huge, existing pump technology is difficult to satisfy the requirement of big flow, adopts the method for many circulating pump parallel connections usually.Especially, an all corresponding cover cleaning solution import and the cleaning solution spray thrower of each circulating pump.Therefore, in this case, flue gas must enter packing section again through too much group of spray thrower.
Flue gas continues upwards to enter packing section from spray section, and purpose is to remove the drop that brings from spray section, or claims the liquid foam, and foam removal efficient is greater than 95%.Packing section has two-layer filler, and all there is one group of water jet every layer of filler top, and in order to the attached solid of flushing foam removal filler Shang , such as gypsum, ammonium sulfate or magnesium sulfate etc. prevent to continue to accumulate the gas passage that stops up in the filler.Under the running status, the water jet operation of lower floor's filler during parking, must move water jet a period of time of upper strata filler continuously, and the water jet of preferred upper and lower layer filler moves 1～5 minute simultaneously.
Be called the purification flue gas through the flue gas after the packing section, directly enter atmosphere from upright chimney by purifying exhanst gas outlet.
From the washing absorption liquid that spray section is got off, directly enter the bubbling segment that is positioned at the desulfurizing tower bottom.At bubbling segment, absorption liquid is through after the air oxidation, and sulphite becomes sulfate, and separates out vitriol under the supersaturation situation.Bubbling segment has also served as the function of desulfurizing agent dissolving tank.Generally speaking, fresh desulfurizing agent is such as the limestone powder slurries of granularity more than the 250-325 order, and magnesia/magnesium carbonate slurries, or liquefied ammonia/vaporous ammonia/ammoniacal liquor directly are added to bubbling segment, mix, dissolve, dilute with absorption liquid.Bubbling segment has also served as the effect of absorption liquid circulating slot, and the absorption liquid that constantly will contain desulfurizing agent through the outer circulating pump of desulfurizing tower is transported to spray section, constantly absorbs the pollutant in the flue gas, especially SO
2, return the bubbling segment of desulfurizing tower bottom.
Simultaneously also must constantly get rid of absorption liquid, enter follow-up sulfate consubstantiality and separate and process equipment, to obtain desulfurization product, solid sulfate salt from bubbling segment.
By above-mentioned disclosed technical scheme as seen, the flue gas desulfurization emission abatement integrated desulfurization tower that is provided with packing section of the present utility model has comprised four parts: be respectively bubbling segment, spray section, packing section and upright chimney from bottom to up, make at desulfurizing tower and deviate from polluter in the flue gas, especially SO
2Afterwards, cleaning of off-gas is without original boiler chimney discharging, thereby it is anticorrosion to have avoided prior art to strengthen boiler chimney, and then do not influence the problem of boiler or electric power ordinary production yet, also saved investment, shorten the duration, and can under lower energy consumption, obtain higher desulfurization and purification efficiency.
Description of drawings
Fig. 1 is the structural representation that is provided with the tower top discharge type flue gas desulfurization tower of packing section.
The specific embodiment
Referring to Fig. 1, tower top discharge type flue gas desulfurization tower of the present utility model is columnar tower, comprising:
Tower body (1); Be arranged on the bubbling segment that is positioned at tower body (2) of tower body (1) bottom, be provided with the air bubbler in the bubbling segment (2) and side is advanced an agitator; Be arranged on the gas approach (3) at tower body (1) middle part, the flow area of gas approach (3) is a rectangle, and the ratio on the minor face of described rectangle and long limit is 0.35; Be arranged on the spray section that is positioned at tower body (4) of tower body (1) middle and upper part, spray section is provided with flue gas distributor in (4), absorption liquid spray thrower and liquid wall stream baffle plate, and described absorption liquid spray thrower is 2 groups; Be arranged on the purification exhanst gas outlet (6) at tower body (1) top;
Be arranged on and purify on the exhanst gas outlet (6), and the upright chimney (7) that directly is connected with exhanst gas outlet (6), the cross-sectional area of upright chimney (7) is circular, and from its air inlet to its exhaust outlet, cross-sectional area constantly reduces, be reduced to 0.125 times with the ratio of tower body cross-sectional area from 0.25, the height of upright chimney (7) is 55 meters;
Described packing section comprises two-layer filler, the below of packing layer and top all are provided with fresh water (FW) rinse spray device, spray thrower comprises distributor pipe and nozzle, distributor pipe is connected with nozzle, distributor pipe is divided into to be responsible for and arm, the person in charge is connected with arm, and the person in charge's internal diameter is 0.2m, and the internal diameter of arm is 0.065mm; Nozzle quantity is, on the cross section of described tower body, arranges 1 nozzle for per 1.0 square metres, and the spout internal diameter of nozzle is 8mm; Packing layer uses the corrugated plastic plate to be arranged in parallel and forms, sheet spacing 25mm, and sheet is 3.0mm, adopts glass fibre enhanced polypropylene plastic production.
Claims (10)
1, a kind of tower top discharge type flue gas desulfurization tower that is provided with packing section, comprise tower body, gas approach on the tower body and exhanst gas outlet, and the upright chimney of exhanst gas outlet connection, it is characterized in that, described tower body inside is provided with packing section, and in the tower body of described packing section between described gas approach and exhanst gas outlet.
2, fume desulfurizing tower according to claim 1 is characterized in that, described packing section comprises two-layer filler.
3, fume desulfurizing tower according to claim 2 is characterized in that, the below of described packing layer is provided with fresh water (FW) rinse spray device.
4, fume desulfurizing tower according to claim 2 is characterized in that, the top of described packing layer is provided with fresh water (FW) rinse spray device.
5, according to claim 3 or 4 described fume desulfurizing towers, it is characterized in that described spray thrower comprises distributor pipe and nozzle, distributor pipe is connected with nozzle, and nozzle is a spiral nozzle.
6, fume desulfurizing tower according to claim 5 is characterized in that, described distributor pipe is divided into to be responsible for and arm, is responsible for to be connected with arm, and the person in charge's internal diameter is 0.1～0.3m, and the internal diameter of arm is 0.05～0.15mm.
7, fume desulfurizing tower according to claim 5 is characterized in that, the quantity of described nozzle is on the cross section of described tower body, to arrange 1 nozzle for per 0.5～2.0 square metre.
8, fume desulfurizing tower according to claim 5 is characterized in that, the spout internal diameter of described nozzle is 5～20mm.
9, fume desulfurizing tower according to claim 2 is characterized in that, described packing layer uses the corrugated plastic plate to be arranged in parallel and forms, sheet spacing 10～50mm, and the thickness of described plate is 2.0mm～3.5mm.
10, fume desulfurizing tower according to claim 9 is characterized in that, the plastic production that described plastic plate adopts glass fibre to strengthen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200554835U CN201179413Y (en) | 2008-02-14 | 2008-02-14 | Column top discharge type flue gas desulfurization column equipped with material filling segment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200554835U CN201179413Y (en) | 2008-02-14 | 2008-02-14 | Column top discharge type flue gas desulfurization column equipped with material filling segment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201179413Y true CN201179413Y (en) | 2009-01-14 |
Family
ID=40248917
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200554835U Expired - Fee Related CN201179413Y (en) | 2008-02-14 | 2008-02-14 | Column top discharge type flue gas desulfurization column equipped with material filling segment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201179413Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101865475A (en) * | 2010-06-07 | 2010-10-20 | 肖成三 | Multifunctional chimney |
| CN106237823A (en) * | 2016-08-31 | 2016-12-21 | 山东万福达化工有限公司 | A kind of efficiently tail gas desulfurization device |
-
2008
- 2008-02-14 CN CNU2008200554835U patent/CN201179413Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101865475A (en) * | 2010-06-07 | 2010-10-20 | 肖成三 | Multifunctional chimney |
| CN106237823A (en) * | 2016-08-31 | 2016-12-21 | 山东万福达化工有限公司 | A kind of efficiently tail gas desulfurization device |
| CN106237823B (en) * | 2016-08-31 | 2022-03-01 | 山东万福达化工有限公司 | High-efficient tail gas desulphurization unit |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201179415Y (en) | Flue gas desulfurization purification column | |
| CN101306317A (en) | Tower top discharge type flue gas desulfurization method | |
| CN201524521U (en) | Large wet desulphurization device with wet-type electrostatic demister | |
| CN101940870B (en) | Device for removing sulfur dioxide in flue gas | |
| CN203108424U (en) | Flue gas treatment apparatus performing desulfurization and denitrification simultaneously | |
| CN105013311A (en) | Flue gas desulfurization dust and mist removal method | |
| CN202010513U (en) | Downstream jet bubbling wet-method desulfurizing device | |
| CN105056746A (en) | Method for realizing boiler flue gas integrated distributed desulfurization and denitrification process | |
| CN101306318A (en) | Tower top discharge type flue gas desulfurization method and desulfurization tower | |
| CN202951399U (en) | Magnesium oxide process desulfurization system | |
| CN108786398B (en) | Flue gas desulfurization and regeneration integrated tower and renewable wet flue gas desulfurization method | |
| CN1597059A (en) | Twin-tower circulation washing and suction smoke and desulfurization method for waste water of power plant boiler | |
| CN101306319A (en) | Direct discharging flue gas treatment method | |
| CN101306316A (en) | Boiler flue gas countercurrent direct purification method | |
| CN201179413Y (en) | Column top discharge type flue gas desulfurization column equipped with material filling segment | |
| CN203469746U (en) | Wet-process desulphurization system with multi-stage humidifying demisting device | |
| CN201195094Y (en) | Smoke purifier with adjacent-line smokestack | |
| CN101549254A (en) | Jacking flue gas processing device and method | |
| CN101791513A (en) | Jacking-type exhaust-gas treatment device and method | |
| CN204522731U (en) | The outer demist wet flue gas desulfurizer of tower | |
| CN201179421Y (en) | Top discharge type flue gas purification column | |
| CN104667721A (en) | Tower top discharge-type desulphurization method and desulfurization tower using the same | |
| CN102553425A (en) | Wet flue gas denitrifying system for coal fired power plant boiler | |
| CN202478813U (en) | Wet flue gas desulphurization system used for coal-fired power plant boiler | |
| CN201179417Y (en) | Exhaust gas desulfurization column |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shenchuan Environment Protection Science and Technology Co., Ltd., Shanghai Assignor: Lou Aijuan Contract fulfillment period: 2009.2.8 to 2011.2.8 Contract record no.: 2009310000011 Denomination of utility model: Column top discharge type flue gas desulfurization column equipped with material filling segment Granted publication date: 20090114 License type: Exclusive license Record date: 20090225 |
|
| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.2.8 TO 2011.2.8; CHANGE OF CONTRACT Name of requester: SHENCHUAN ENVIRONMENT PROTECTION TECH CO., LTD., S Effective date: 20090225 |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shenchuan Environment Protection Science and Technology Co., Ltd., Shanghai Assignor: Lou Aijuan Contract fulfillment period: 2009.4.9 to 2016.4.9 Contract record no.: 2009310000102 Denomination of utility model: Column top discharge type flue gas desulfurization column equipped with material filling segment Granted publication date: 20090114 License type: Exclusive license Record date: 20090619 |
|
| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.4.9 TO 2016.4.9; CHANGE OF CONTRACT Name of requester: SHENCHUAN ENVIRONMENT PROTECTION TECH CO., LTD., S Effective date: 20090619 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090114 Termination date: 20160214 |