CN105498488A - 一种烟气处理方法 - Google Patents
一种烟气处理方法 Download PDFInfo
- Publication number
- CN105498488A CN105498488A CN201510823665.7A CN201510823665A CN105498488A CN 105498488 A CN105498488 A CN 105498488A CN 201510823665 A CN201510823665 A CN 201510823665A CN 105498488 A CN105498488 A CN 105498488A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- flue
- oxygen
- copper
- hydrogen peroxide
- Prior art date
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 239000003546 flue gas Substances 0.000 title claims abstract description 59
- MHAJPDPJQMAIIY-UHFFFAOYSA-N hydrogen peroxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 56
- 239000001301 oxygen Substances 0.000 claims abstract description 41
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 41
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- 238000005507 spraying Methods 0.000 claims abstract description 9
- 239000012288 hydrogen peroxide Substances 0.000 claims abstract 8
- 241001081830 Degeneriaceae Species 0.000 claims abstract 2
- 229910052904 quartz Inorganic materials 0.000 claims description 33
- 239000010453 quartz Substances 0.000 claims description 33
- 229960002163 hydrogen peroxide Drugs 0.000 claims description 28
- 238000003672 processing method Methods 0.000 claims description 23
- 238000000889 atomisation Methods 0.000 claims description 12
- 238000006243 chemical reactions Methods 0.000 claims description 7
- 239000000779 smoke Substances 0.000 claims description 7
- 229910001885 silicon dioxide Inorganic materials 0.000 claims 5
- 238000006477 desulfuration reactions Methods 0.000 abstract description 12
- 230000003009 desulfurizing Effects 0.000 abstract description 12
- ARUVKPQLZAKDPS-UHFFFAOYSA-L Copper(II) sulfate Chemical compound 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[Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 abstract 4
- 229910000365 copper sulfate Inorganic materials 0.000 abstract 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials 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- 229910002089 NOx Inorganic materials 0.000 description 6
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- PMZURENOXWZQFD-UHFFFAOYSA-L sodium sulphate Substances 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[Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound 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OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Chemical compound 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[Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 229910052815 sulfur oxide Inorganic materials 0.000 description 2
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- SUKJFIGYRHOWBL-UHFFFAOYSA-N Sodium hypochlorite Chemical compound 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- 239000003500 flue dust Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003000 nontoxic Effects 0.000 description 1
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- 238000011017 operating method Methods 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/007—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
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Abstract
本发明公开一种烟气处理方法,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为50-70℃的烟气通过烟气管道(1),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。本发明还公开了一套用于烟气处理方法的装置:在烟气管道(1)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(1)的管壁上,分别设置过氧化氢入口(3)、氧气入口(4)、硫酸铜溶液入口(5)。本发明的烟气处理方法,能同时脱硫脱硝,且操作简单,效率高。
Description
技术领域
[0001]本发明属于燃煤烟气处理领域,具体涉及一种烟气处理方法。
背景技术
[0002]我国煤炭资源丰富,是主要的能量来源之一,但是随着煤炭的使用,环境问题凸显,煤炭的燃烧向外排放烟气,烟气中含有大量的SOx、SO2、N20等污染气体。据统计大气污染物中SOx的90%、C0的71%、C02的85%、Ν0χ的70%和烟尘的70%都来自原煤的直接燃烧,因此燃煤烟气是形成我国大气污染的主要原因。为进一步改善城市环境空气质量,加强燃煤蒸汽锅炉污染治理,急需寻找一种高效的烟气脱硫脱硝方法。而现有技术中,多数都是重视烟气的脱硫,不能同时进行脱硫脱销,且操作繁琐。
[0003] NOx在阳光的作用下会引起光化学反应,形成光化学烟雾,从而造成严重的大气污染,因此烟气脱硝与脱硫同样不容忽视。烟气脱硝,是指把已生成的NOx还原,从而脱除烟气中的NOx,按治理工艺可分为湿法脱硝和干法脱硝。主要包括:氧化吸收法、选择性非催化还原法、吸附法、离子体活化法等。在氧化吸收法中,将NO转换为NOx的难度较大,所以此类方法氧化剂的选择和制备是研究的核心。目前研究较多的氧化剂有HC103、NaC102、03、H202和KMnO4等。由于过氧化氢无毒且无二次污染,对它的研究更多。但是现有技术中,利用过氧化氢处理烟气的技术还存在效率不高,操作复杂等问题。
发明内容
[0004]针对现有技术存在的问题,本发明提供一种高效的烟气处理方法,能同时脱硫脱硝。
[0005]本发明的技术方案如下:
[0006] —种烟气处理方法,包括以下步骤:打开紫外线灯管开关,使紫外线灯管处于工作状态,将温度为50_70°C的烟气通过烟气管道,同时分别通过过氧化氢入口喷入雾化的过氧化氢溶液、通过氧气入口通入氧气、通过硫酸铜溶液入口喷入雾化的硫酸铜溶液,与烟气混合反应。
[0007]所述紫外线灯管的紫外线波长为320-380nm。
[0008]所述过氧化氢溶液浓度为10_15ppm。
[0009]所述氧气的纯度为99%以上,如:医用氧气等。控制氧气在烟气管道中的浓度为0.1-0.3mol/L0
[0010] 所述硫酸铜溶液浓度为5-15ppm。
[0011] —套用于以上所述烟气处理方法的装置,在烟气管道中设置紫外线灯管,在靠近烟气入口的烟气管道的管壁上,分别设置过氧化氢入口、氧气入口、硫酸铜溶液入口。
[0012]所述烟气管道中设置的紫外线灯管根据需要在烟气管道内壁不同位置设置多条,优选在烟气管道中设置4条紫外线灯管,分别位于烟气管道内部管壁的上方、下方、左方、右方。
[0013]工作时,排放的烟气经过烟气降温器降温至50_70°C后,在烟气管道内设置的紫外线灯管的照射中,将过氧化氢溶液、硫酸铜溶液通过雾化喷嘴喷入管道内与烟气混合,同时通入适量的氧气调节氧的浓度。在强氧化的作用下,烟气中的NO转化为NOx,例如NO2等,进而再将NOx与H2O反应生成NO3—;另外,在强氧化的作用下,将SO2氧化为硫酸,其化学反应方程式为:H202+S02 = H2S04。回收时,加入氢氧化钠溶液,NO3—和S042—与氢氧化钠反应,生成硫酸钠和碳酸钠进行回收,同时对烟气进行脱硫脱销。
[0014]本发明的有益效果为:
[0015] 1.本发明的烟气处理方法,能同时脱硫脱硝,通过加入氧气并控制了适合的浓度,加入金属离子起催化作用,大大提高了脱硫脱销效率,脱硫率90%以上,脱硝率95%以上,消除烟气对大气的污染;
[0016] 2.本发明的烟气处理方法,处理后生成硫酸钠和碳酸钠等产物,能进行回收利用;
[0017] 3.本发明的烟气处理方法,操作步骤不繁琐,成本低,容易推广应用。
附图说明
[0018]图1为烟气管道结构示意图。
[0019]图2为烟气管道截面示意图。
[0020]图中:1.烟气管道、2.紫外线灯管、3.过氧化氢入口、4.氧气入口、5.硫酸铜溶液入P
具体实施方式
[0021]下面结合具体实施例对本发明作进一步描述,但不限制本发明的保护范围和应用范围:
[0022] 实施例1
[0023] 一种烟气处理方法,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为50°C的烟气通过烟气管道(I),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。
[0024]所述紫外线灯管(2)的紫外线波长为380nm。
[0025]所述过氧化氢溶液浓度为lOppm。
[0026]所述氧气为纯氧气,控制氧气在烟气管道(I)中的浓度为0.lmol/L。
[0027] 所述硫酸铜溶液浓度为15ppm。
[0028]用于上述烟气处理方法的装置:在烟气管道(I)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(I)的管壁上,分别设置过氧化氢入口(3)、氧气入口(4)、硫酸铜溶液入口(5)0
[0029]所述烟气管道(I)中设置4条紫外线灯管(2),分别位于烟气管道(I)内部管壁的上方、下方、左方、右方。
[0030] 经测定,本实施例的脱硫率为92.56%,脱硝率为96.12%。
[0031] 实施例2
[0032] 一种烟气处理方法,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为70°C的烟气通过烟气管道(I),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。
[0033]所述紫外线灯管(2)的紫外线波长为320nm。
[0034]所述过氧化氢溶液浓度为15ppm。
[0035]所述氧气的纯度为99.5%,控制氧气在烟气管道(I)中的浓度为0.3mol/L。
[0036] 所述硫酸铜溶液浓度为5ppm。
[0037]用于上述烟气处理方法的装置:在烟气管道(I)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(I)的管壁上,分别设置过氧化氢入口(3)、氧气入口(4)、硫酸铜溶液入口(5)0
[0038]所述烟气管道(I)中设置4条紫外线灯管(2),分别位于烟气管道(I)内部管壁的上方、下方、左方、右方。
[0039] 经测定,本实施例的脱硫率为93.07%,脱硝率为95.08 %。
[0040] 实施例3
[0041] —种烟气处理方法,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为55°C的烟气通过烟气管道(I),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。
[0042]所述紫外线灯管(2)的紫外线波长为350nm。
[0043]所述过氧化氢溶液浓度为12ppm。
[0044]所述氧气的纯度为99.5%,控制氧气在烟气管道(I)中的浓度为0.2mol/L。
[0045] 所述硫酸铜溶液浓度为lOppm。
[0046]用于上述烟气处理方法的装置:在烟气管道(I)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(I)的管壁上,分别设置过氧化氢入口(3)、氧气入口(4)、硫酸铜溶液入口(5)0
[0047]所述烟气管道(I)中设置4条紫外线灯管(2),分别位于烟气管道(I)内部管壁的上方、下方、左方、右方。
[0048] 经测定,本实施例的脱硫率为93.14%,脱硝率为96.23%。
[0049] 实施例4
[0050] —种烟气处理方法,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为60°C的烟气通过烟气管道(I),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。
[0051]所述紫外线灯管(2)的紫外线波长为360nm。
[0052]所述过氧化氢溶液浓度为13ppm。
[0053]所述氧气为纯氧气,控制氧气在烟气管道(I)中的浓度为0.2mol/L。
[0054] 所述硫酸铜溶液浓度为13ppm。
[0055]用于上述烟气处理方法的装置:在烟气管道(I)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(I)的管壁上,分别设置过氧化氢入口(3)、氧气入口(4)、硫酸铜溶液入口(5)0
[0056]所述烟气管道(I)中设置4条紫外线灯管(2),分别位于烟气管道(I)内部管壁的上方、下方、左方、右方。
[0057] 经测定,本实施例的脱硫率为96.05%,脱硝率为98.98 %。
Claims (7)
1.一种烟气处理方法,其特征在于,包括以下步骤:打开紫外线灯管(2)开关,使紫外线灯管(2)处于工作状态,将温度为50-70°C的烟气通过烟气管道(I),同时分别通过过氧化氢入口(3)喷入雾化的过氧化氢溶液、通过氧气入口(4)通入氧气、通过硫酸铜溶液入口(5)喷入雾化的硫酸铜溶液,与烟气混合反应。
2.根据权利要求1所述的烟气处理方法,其特征在于:所述紫外线灯管(2)的紫外线波长为 320-380nm。
3.根据权利要求1所述的烟气处理方法,其特征在于:所述过氧化氢溶液浓度为10-15ppm0
4.根据权利要求1所述的烟气处理方法,其特征在于:所述氧气的纯度为99%以上,控制氧气在烟气管道(I)中的浓度为0.1-0.3mol/L。
5.根据权利要求1所述的烟气处理方法,其特征在于:所述硫酸铜溶液浓度为5-15ppm。
6.一套用于权利要求1所述烟气处理方法的装置,其特征在于:在烟气管道(I)中设置紫外线灯管(2),在靠近烟气入口的烟气管道(I)的管壁上,分别设置过氧化氢入口(3)、氧气入口( 4)、硫酸铜溶液入口( 5)。
7.根据权利要求6所述烟气处理方法的装置,其特征在于:所述烟气管道(I)中设置4条紫外线灯管(2),分别位于烟气管道(I)内部管壁的上方、下方、左方、右方。
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CN105435633A (zh) * | 2015-11-24 | 2016-03-30 | 广西阔能霸能源科技开发有限责任公司 | 一种燃煤烟气处理工艺 |
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CN105457460A (zh) * | 2015-11-24 | 2016-04-06 | 广西阔能霸能源科技开发有限责任公司 | 一种高效烟气处理工艺及装置 |
CN105477986A (zh) * | 2015-11-24 | 2016-04-13 | 广西阔能霸能源科技开发有限责任公司 | 一种烟气处理工艺及装置 |
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