CN204275782U - A kind of NOx based on SNCR-SCR coupling combines with mercury and removes device - Google Patents
A kind of NOx based on SNCR-SCR coupling combines with mercury and removes device Download PDFInfo
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- CN204275782U CN204275782U CN201420684016.4U CN201420684016U CN204275782U CN 204275782 U CN204275782 U CN 204275782U CN 201420684016 U CN201420684016 U CN 201420684016U CN 204275782 U CN204275782 U CN 204275782U
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- mercury
- sncr
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- ammonium chloride
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Abstract
A kind of NOx based on SNCR-SCR coupling not increasing the equipment of removing of the utility model combines with mercury and removes device, comprises control system, and the SNCR system connected successively, burner hearth, SCR system and smoke processing system; SNCR system comprises the solution reservoir and compressed air cylinder that are attempted by burner hearth spout input, is connected to the dissolving tank of the input of solution reservoir, and is connected in parallel on the urea warehouse of dissolving tank input, ammonium chloride warehouse and sweet-water tank; Smoke processing system comprises the wet desulfuration tower being connected to SCR system exhaust end; Control system comprises industrial computer, and the urea metering units being arranged on the urea warehouse port of export be connected with industrial computer respectively, be arranged on the ammonium chloride metering units of the ammonium chloride warehouse port of export, be arranged on the injection metering module of burner hearth spout input, be arranged on the Elemental Mercury checkout gear of wet desulfuration tower exhaust outlet and be arranged on the nitrogen oxide checkout gear of the SCR system port of export.
Description
Technical field
The utility model relates to the filed of flue gas purification of coal-burning power plant's pollutant cooperation-removal, is specially a kind of NOx based on SNCR-SCR coupling and combines with mercury and remove device.
Background technology
Environment and resources problem is the key subjects of face of mankind nowadays, and the pollution that a large amount of uses of the fossil fuel such as coal, oil and natural gas bring and the deterioration of the ecological environment increase the weight of day by day.Mercury is a kind of hypertoxic pollutant, and coal fire discharged mercury is one of main source of artificial mercury pollution, when mercury emissions is in air, will cause serious harm.Under the effect of microorganism, mercury can be transformed into the stronger methyl mercury of a kind of toxicity, run up in intelligent's body by food chain, because mercury is to the height affinity of sulfur-containing compound, can destructive enzyme and other oroteins function and affect it and again synthesize, cause the damage of kidney and liver even various serious consequence such as exhaustion thus.In addition, mercury is also a kind of neurotoxin, can be accumulated in cerebral tissue, causes human motion imbalance, aphasis etc.
Mercury is ubiquitous a kind of trace element in coal, and its average content is about 0.1ppm.Mercury exists with forms such as organic, element state, sulphided state and selenides in coal, and pyrite and cinnabar are the main host plants of mercury in coal.High-temp combustion region in the boiler, most mercury discharges from coal with the form of mercury vapour.In control before can being divided into burning to the emission control of mercury, burning, control and tail flue gas control three kinds, existing research finds that the active carbon removal of mercury is one of the most promising technology in tail flue gas Mercury vacancy, but the active carbon mainly coal mass active carbon used at present, the key issue that restriction active carbon is applied in demercuration is that charcoal absorption amount is lower, cost is high, and need to increase new attached removal of mercury equipment, thus economy is poor.
In pollutant catabolic gene equipment (APCDs), mercury removes the existing forms depending primarily on Mercury In Coal Combustion Flue Gas.Mercury In Coal Combustion Flue Gas exists with element mercury, mercury oxide and particle mercury three kinds of forms usually.Particle mercury can be removed together with particle in the particle control appliances (PMCD) such as electrostatic precipitator (ESP), sack cleaner (FF).Oxidation state mercury is soluble in water, at desulphurization system (FGD), especially can be removed in wet desulfurization system (WFGD); It is also easy to be adsorbed on the particle such as flying dust and dry-desulphurizer and forms particle mercury, and then is removed by particle control appliance.On the contrary, Elemental Mercury highly volatile, also water insoluble, make the mercury in flue gas be difficult to be desulfurized, denitrification apparatus cooperation-removal, therefore cannot rely on the pollutant catabolic gene equipment (APCDs) that existing coal-burning power plant is arranged in combustion back zone, the desulphurization system (FGD) of such as electrostatic precipitation system (ESP), bag-type dust removal system (FF), wet method or dry method, SCR (SCR) and SNCR (SNCR) equipment etc. carry out cooperation-removal.
Utility model content
For problems of the prior art, the utility model provides a kind of removal efficiency to Elemental Mercury large, does not increase extra to remove equipment, and the NOx based on SNCR-SCR coupling realizing cooperation-removal combines with mercury and removes device.
The utility model is achieved through the following technical solutions:
To combine with mercury based on the NOx of SNCR-SCR coupling and remove a device, comprise control system, and the SNCR system connected successively, burner hearth, SCR system and smoke processing system; SNCR system comprises the solution reservoir and compressed air cylinder that are attempted by burner hearth spout input, is connected to the dissolving tank of the input of solution reservoir, and is connected in parallel on the urea warehouse of dissolving tank input, ammonium chloride warehouse and sweet-water tank; Smoke processing system comprises the wet desulfuration tower being connected to SCR system exhaust end; Control system comprises industrial computer, and the urea metering units being arranged on the urea warehouse port of export be connected with industrial computer respectively, be arranged on the ammonium chloride metering units of the ammonium chloride warehouse port of export, be arranged on the injection metering module of burner hearth spout input, be arranged on the Elemental Mercury checkout gear of wet desulfuration tower exhaust outlet and be arranged on the nitrogen oxide checkout gear of the SCR system port of export; The elemental mercury concentration feedback signal that the input access of industrial computer sends from Elemental Mercury checkout gear and the nitrous oxides concentration feedback signal that nitrogen oxide checkout gear sends, the output of industrial computer connects urea metering units respectively, the control end of ammonium chloride metering units and injection metering module.
Preferably, control system is also included in roof of the furnace installation infrared high-speed camera, and it is for receiving the infrared energy of fly ash granule in burner hearth and dust and respective signal being linked into the input of industrial computer.
Preferably, smoke processing system also comprises the electric cleaner being connected to wet desulfuration tower incoming end, and is arranged on wet desulfuration tower outlet side chimney.
Further, between electric cleaner and wet desulfuration tower, air-introduced machine is set
Compared with prior art, the utility model has following useful technique effect:
Described in the utility modelly remove device, by adding with urea storage in SNCR system and dissolving consistent ammonium chloride and store dissolution equipment, thus not only can ensure that the quantity delivered of ammonia in the reducing agent when spraying into burner hearth, and while not introducing other foreign ions, add the production of HCl, thus the oxidation completed when can carry out further denitration in follow-up SCR system Elemental Mercury, by follow-up smoke processing system, the bivalent mercury after oxidation is removed again, thus can realize realizing removing Elemental Mercury on the basis of existing pollutant handling arrangement, structure is simple, design ingenious, easy to use, with low cost.By respectively to the detection of Elemental Mercury and nitrous oxides concentration, thus the ratio of ammonium chloride and urea in reducing agent mixed solution can be obtained, thus can regulate respectively both, reducing agent can not only be made full use of and carry out removing of nitrogen oxide, HCl is utilized to carry out fully oxidized to Elemental Mercury, avoid waste, and can by the control to ammonium chloride, prevent the excessive of HCl and to the corrosion of upstream device with bring new pollution, realize the removing of nitrogen oxide, the efficient oxidation of Elemental Mercury and the balance that reduces between upstream device corrosion.
Further, by at roof of the furnace installation infrared high-speed camera, can position by the more accurate reducing agent mixed solution to spraying into, ensure that it decomposes and reaction effect, the amount of each spout ammonium chloride, urea and demineralized water can be adjusted according to flue-gas temperature, improve the denitration efficiency of system, reduce the escaping of ammonia, better ammonium chloride is carried out even thermal decomposition, ensure steadily carrying out smoothly of subsequent reactions.
Further, utilize electric cleaner before flue gas enters wet desulphurization, adsorbing and removing can be carried out to the solid-state mercury wherein existed in granular form, improve the removal efficiency of system to mercury better, and reduce in wet desulfuration tower mercuric percent reduction that is cured.
Accompanying drawing explanation
Fig. 1 is for removing the structural representation of device described in the utility model example.
In figure: 1 is urea warehouse, 2 is ammonium chloride warehouse, and 3 is sweet-water tank, and 4 is compressed air cylinder, 51 is urea metering units, and 52 is ammonium chloride metering units, and 6 is dissolving tank, 7 is solution reservoir, and 8 for spraying metering module, and 9 is SCR system, 10 is electric cleaner, and 11 is air-introduced machine, and 12 is wet desulfuration tower, 13 is chimney, 14 Elemental Mercury checkout gears, and 15 is nitrogen oxide checkout gear, 16 is infrared high-speed video camera, and 17 is industrial computer, and 18 is burner hearth.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described in further detail, described in be to explanation of the present utility model instead of restriction.
A kind of NOx based on SNCR-SCR coupling of the utility model combines with mercury and removes device, and as shown in Figure 1, it comprises control system, and the SNCR system connected successively, burner hearth 18, SCR system 9 and smoke processing system; SNCR system comprises the solution reservoir 7 and compressed air cylinder 4 that are attempted by burner hearth 18 spout input, is connected to the dissolving tank 6 of the input of solution reservoir 7, and is connected in parallel on the urea warehouse 1 of dissolving tank 6 input, ammonium chloride warehouse 2 and sweet-water tank 3; Smoke processing system comprises the wet desulfuration tower 12 being connected to SCR system 9 exhaust end; Control system comprises industrial computer 17, and the urea metering units 51 being arranged on urea warehouse 1 port of export be connected with industrial computer 17 respectively, be arranged on the ammonium chloride metering units 52 of ammonium chloride warehouse 2 port of export, be arranged on the injection metering module 8 of burner hearth 18 spout input, be arranged on the Elemental Mercury checkout gear 14 of wet desulfuration tower 12 exhaust outlet and be arranged on the nitrogen oxide checkout gear 15 of SCR system 9 port of export; The elemental mercury concentration feedback signal that the input access of industrial computer 17 sends from Elemental Mercury checkout gear 14 and the nitrous oxides concentration feedback signal that nitrogen oxide checkout gear 15 sends, the output of industrial computer 17 connects urea metering units 51 respectively, the control end of ammonium chloride metering units 52 and injection metering module 8.
As shown in Figure 1, control system is also included in burner hearth 18 top installation infrared high-speed camera 16, and it is for receiving the infrared energy of fly ash granule in burner hearth 18 and dust and respective signal being linked into the input of industrial computer 17.As shown in Figure 1, smoke processing system also comprises the electric cleaner 10 being connected to wet desulfuration tower 12 incoming end by air-introduced machine 11, and is arranged on wet desulfuration tower 12 outlet side chimney 13.
The utility model is by SNCR system, identical with urea dissolution equipment with chloride leach equipment by arranging, can be common as reducing agent using both, make it in follow-up SCR system during denitration, the HCl that ammonium chloride can be utilized to produce is oxidized Elemental Mercury under the effect of SCR catalyst, thus can be bivalent mercury by the elemental mercury oxidation of at least 95%; Realize absorbing and removing to bivalent mercury by follow-up wet desulfuration tower again, therefore, it is possible under the condition not increasing the new equipment that removes, utilize the conventional existing pollutant catabolic gene device of power plant to realize the efficient removal of nitrogen oxide and mercury, simple to operate, with low cost, successful, is applicable to the current national conditions of China.
Utilize mercury removal device described in the utility model concrete when carrying out the removing of Elemental Mercury in flue gas, step is as follows,
1) roof of the furnace installs an infrared high-speed video camera, fly ash granule in reception stove and the infrared energy of dust, in conjunction with radiation against cigarette temperature in theory of solving on-line monitoring stove, according to the eject position being adjusted each spout ammonium chloride, urea by cigarette temperature in stove, improve the denitration efficiency of system.
2) checkout gear of Elemental Mercury is set after desulfurizer, mercury concentration in flue gas after real-time detection desulfurizer, feedback signal controls by industrial computer 17 addition that ammonium chloride metering units 52 regulates NH4Cl, nitrogen oxide checkout gear is set after SCR system 9, the NOx concentration in flue gas can be detected in real time, control by industrial computer 17 emitted dose mixing reductant solution.
3) in SNCR system, urea and ammonium chloride are stored in urea warehouse 1 and ammonium chloride warehouse 2 respectively, urea and a certain amount of ammonium chloride are added to dissolving tank 6 li, with demineralized water two dissolution of solids are become the total mass concentration of solute be 40 ~ 60% mixing reductant solution, be transported in solution reservoir 7 by solution feeding pump.
4) mixing reductant solution is sprayed into the hearth region that temperature is 820 ~ 1250 DEG C, urea thermal decomposition goes out NH
3and carry out reaction with the NOx in flue gas and generate N
2and H
2o; NH
4cl resolves into NH
3and HCl, obtain including HCl and unreacted NH
3tail gas, the addition of the reductant solution of mixing is controlled by the injection metering module 8 arranged in SNCR system, this module adopts independently chemical agent flow-control, Field pressure control valve combined with PLC on the spot and responds the control signal that industrial computer 17 sends, regulating the reducing agent flow of mixing.
5) tail gas of burner hearth 18 is passed in the denitrification apparatus of SCR system 9, unreacted NH
3continue to carry out reaction with the NOx in flue gas as reducing agent and generate N
2and H
2elemental mercury oxidation in flue gas is become bivalent mercury by O, HCl under the effect of SCR catalyst.
6) enter containing mercuric flue gas in the wet desulfuration tower 12 in wet desulfurization system, bivalent mercury is dissolved in the gypsum slurries in wet desulfuration tower 12, completes the oxidation removal of gaseous elemental mercury.
7) for improving the demercuration efficiency of WFGD system, the mercuric vulcanized sodium additive of solidification is added to the pulping system of desulfurizing agent, enter in desulfurizing tower by pulping system, most bivalent mercury is proceeded in desulfurated plaster, make mercury " discharging again " be reduced to minimum level.
Wherein, the mixing reductant solution of urea and ammonium chloride enters spray gun via injection metering module 8, and sprays into the hearth region that temperature is 850 ~ 1100 DEG C, and now carbamide reducing agent can go out NH by rapid thermal decomposition
3and carry out reaction with the NOx in flue gas and generate N
2and H
2o, substantially not with the O in flue gas
2reaction, its key reaction is:
CO(NH
2)
2→2NH
2+CO (1)
NH
2+NOx→N
2+H
2O (2)
CO+NOx→N
2+CO
2(3)
NH under high temperature
4cl resolves into NH
3and HCl, NH wherein
3can be used as denitrification reducing agent, due to NH
4cl comparatively stablizes and safe chemical reagent, uses NH
4cl solution is both for SNCR denitration provides safe NH
3supply, simultaneously also for the oxidation of mercury provides halid source, realizes denitration, removal of mercury integration.
After wet desulfuration tower 12, arrange the checkout gear 14 of Elemental Mercury, detect the mercury concentration in the flue gas after desulfurizer in real time, feedback signal is by industrial computer 17 control NH
4the addition of Cl, arranges nitrogen oxide checkout gear 15 after SCR system 9, can detect the NOx concentration in flue gas in real time, be controlled the emitted dose of carbamide reducing agent by industrial computer 17.The chemical equation of its foundation and amount of substance are than as follows:
NH
4Cl→NH
3+HCl (4)
4NH
3+4NO+O
2→4N
2+6H
2O (5)
4NH
3+2NO+2O
2→3N
2+6H
2O (6)
8NH
3+6NO→7N
2+12H
2O (7)
The utility model adopts the combined denitration device of SNCR+SCR, by the adjustment of straying quatity between urea and ammonium chloride solution spraying system different layers, by both operations, organically combines acting in conjunction, reaches the NOx emission reduction effect of more than 85%.Meanwhile, the NH that under the high temperature of the mixing reductant solution utilizing SNCR system to provide in burner hearth 18, pyrolysis produces
3both can as the reducing agent of SNCR system, NOx in flue gas is decomposed into N by unnecessary ammonia under the effect of the catalyst of SCR system 9 within the scope of the flue-gas temperature of 320 DEG C ~ 400 DEG C
2and H
2o.Produce HCl under the effect of SCR catalyst, by flue gas more than 95% Elemental Mercury (Hg
0) be oxidized to bivalent mercury (HgCl
2), its oxidation reaction is as follows:
In flue gas after SCR denitration system 9, the Elemental Mercury of more than 95% is converted into the mercury of divalent state, and enters electric cleaner 10 and wet desulfuration tower 12 successively along with flue gas.
Conventional electric cleaner (ESP) is under HVDC electro ultrafiltration, make cathode line corona discharge, electric field space is full of negative electrical charge, and the particulate Hg being attached to flue dust surface enters adion after electric field and charged, and under electric field force effect, pole plate moves and is captured on the sunny side.The mercury oxide of gaseous state is soluble in water, can be removed by WFGD.The solid-state mercury existed in granular form in flue gas and bivalent mercury soluble in water remove by existing electric cleaner 10 and wet desulfuration tower 12 by the utility model, and the removal efficiency of total mercury is more than 95%.For suppressing the secondary reduction release of mercury in WFGD system, this patent adds solidification mercuric vulcanized sodium additive the pulping system of desulfurizing agent to, enter in wet desulfuration tower 12 by pulping system, most bivalent mercury is proceeded in desulfurated plaster, makes mercury " discharging again " be reduced to minimum level.
Finally, the flue gas after dedusting, desulphurization and denitration, demercuration enters air by chimney 13 under the effect of air-introduced machine 11, completes while removing nitrogen and sulphur on existing equipment basis, the combined synchronization of Elemental Mercury is removed, rational in infrastructure, arrange ingenious, with low cost, successful.
The SNCR-SCR combined system that the utility model adopts, again without the need to arranging static mixer, ammonia injection grid, without the need to lengthening flue, the catalyst used wants much less compared with being used alone SCR denitration system, the demand to elemental mercury oxidation can be met simultaneously, and the NOx removal efficiency of more than 85% can be reached, more than 95% removal efficiency to mercury, reduce blocking and the corrosion of upstream device; And SCR reactor volume is little, therefore stronger to space adaptability; Do not increase the extra equipment that removes and the directly additional interpolation equipment in SCR system, make denitrating system resistance little, also reduce operation power consumption.
Claims (4)
1. to combine with mercury based on the NOx of SNCR-SCR coupling and remove a device, it is characterized in that, comprise control system, and the SNCR system connected successively, burner hearth (18), SCR system (9) and smoke processing system;
Described SNCR system comprises the solution reservoir (7) and compressed air cylinder (4) that are attempted by burner hearth (18) spout input, be connected to the dissolving tank (6) of the input of solution reservoir (7), and be connected in parallel on the urea warehouse (1) of dissolving tank (6) input, ammonium chloride warehouse (2) and sweet-water tank (3);
Described smoke processing system comprises the wet desulfuration tower (12) being connected to SCR system (9) exhaust end;
Described control system comprises industrial computer (17), and the urea metering units (51) being arranged on urea warehouse (1) port of export be connected with industrial computer (17) respectively, be arranged on the ammonium chloride metering units (52) of ammonium chloride warehouse (2) port of export, be arranged on the injection metering module (8) of burner hearth (18) spout input, be arranged on the Elemental Mercury checkout gear (14) of wet desulfuration tower (12) exhaust outlet and be arranged on the nitrogen oxide checkout gear (15) of SCR system (9) port of export; The elemental mercury concentration feedback signal that the input access of industrial computer (17) sends from Elemental Mercury checkout gear (14) and the nitrous oxides concentration feedback signal that nitrogen oxide checkout gear (15) sends, the output of industrial computer (17) connects urea metering units (51) respectively, the control end of ammonium chloride metering units (52) and injection metering module (8).
2. a kind of NOx based on SNCR-SCR coupling according to claim 1 combines with mercury and removes device, it is characterized in that, described control system is also included in burner hearth (18) top installation infrared high-speed camera (16), and it is for receiving the infrared energy of fly ash granule in burner hearth (18) and dust and respective signal being linked into the input of industrial computer (17).
3. a kind of NOx based on SNCR-SCR coupling according to claim 1 combines with mercury and removes device, it is characterized in that, described smoke processing system also comprises the electric cleaner (10) being connected to wet desulfuration tower (12) incoming end, and is arranged on wet desulfuration tower (12) outlet side chimney (13).
4. a kind of NOx based on SNCR-SCR coupling according to claim 3 combines with mercury and removes device, it is characterized in that, arranges air-introduced machine (11) between described electric cleaner (10) and wet desulfuration tower (12).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420684016.4U CN204275782U (en) | 2014-11-14 | 2014-11-14 | A kind of NOx based on SNCR-SCR coupling combines with mercury and removes device |
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|---|---|---|---|
| CN201420684016.4U CN204275782U (en) | 2014-11-14 | 2014-11-14 | A kind of NOx based on SNCR-SCR coupling combines with mercury and removes device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104399360A (en) * | 2014-11-14 | 2015-03-11 | 华能国际电力股份有限公司 | NOx and mercury combined removal process and device based on combination of SNCR-SCR |
| CN105251326A (en) * | 2015-10-09 | 2016-01-20 | 广州特种承压设备检测研究院 | Reduction and oxidation combined denitration system and denitration method thereof |
| WO2022193557A1 (en) * | 2021-03-15 | 2022-09-22 | 苏州西热节能环保技术有限公司 | Halogen injection system for synergistic mercury removal of flue gas |
-
2014
- 2014-11-14 CN CN201420684016.4U patent/CN204275782U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104399360A (en) * | 2014-11-14 | 2015-03-11 | 华能国际电力股份有限公司 | NOx and mercury combined removal process and device based on combination of SNCR-SCR |
| CN105251326A (en) * | 2015-10-09 | 2016-01-20 | 广州特种承压设备检测研究院 | Reduction and oxidation combined denitration system and denitration method thereof |
| WO2022193557A1 (en) * | 2021-03-15 | 2022-09-22 | 苏州西热节能环保技术有限公司 | Halogen injection system for synergistic mercury removal of flue gas |
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