CN101337153A - 超声波一体化脱硫脱硝脱汞方法及其装置 - Google Patents
超声波一体化脱硫脱硝脱汞方法及其装置 Download PDFInfo
- Publication number
- CN101337153A CN101337153A CNA2008100216142A CN200810021614A CN101337153A CN 101337153 A CN101337153 A CN 101337153A CN A2008100216142 A CNA2008100216142 A CN A2008100216142A CN 200810021614 A CN200810021614 A CN 200810021614A CN 101337153 A CN101337153 A CN 101337153A
- Authority
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- China
- Prior art keywords
- ultrasonic
- bed reactor
- bubbling bed
- flue gas
- desulfurization denitration
- Prior art date
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- 230000003009 desulfurizing Effects 0.000 title claims abstract description 20
- 238000006477 desulfuration reactions Methods 0.000 title claims description 20
- 238000006243 chemical reactions Methods 0.000 claims abstract description 54
- 230000005587 bubbling Effects 0.000 claims abstract description 43
- 230000001702 transmitter Effects 0.000 claims abstract description 26
- 230000000694 effects Effects 0.000 claims abstract description 23
- 239000000498 cooling water Substances 0.000 claims abstract description 15
- 229910052813 nitrogen oxides Inorganic materials 0.000 claims abstract description 10
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000002253 acids Substances 0.000 claims abstract description 8
- 239000000428 dust Substances 0.000 claims abstract description 7
- 238000007254 oxidation reactions Methods 0.000 claims abstract description 7
- 239000003337 fertilizer Substances 0.000 claims abstract description 6
- 229910001385 heavy metals Inorganic materials 0.000 claims abstract description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical class 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 6
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 56
- 239000003546 flue gases Substances 0.000 claims description 56
- 239000007789 gases Substances 0.000 claims description 18
- 239000000376 reactants Substances 0.000 claims description 14
- 238000001816 cooling Methods 0.000 claims description 12
- 239000000047 products Substances 0.000 claims description 12
- 238000000034 methods Methods 0.000 claims description 11
- 229910001874 nitric oxide Inorganic materials 0.000 claims description 9
- 230000015572 biosynthetic process Effects 0.000 claims description 8
- 238000005755 formation reactions Methods 0.000 claims description 8
- 239000003814 drugs Substances 0.000 claims description 7
- -1 hydroxyl radical free radical Chemical class 0.000 claims description 7
- 239000007788 liquids Substances 0.000 claims description 7
- 239000000203 mixtures Substances 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 7
- 230000003647 oxidation Effects 0.000 claims description 6
- 230000001590 oxidative Effects 0.000 claims description 6
- 239000002826 coolants Substances 0.000 claims description 5
- 239000000284 extracts Substances 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- 239000011901 water Substances 0.000 claims description 4
- 239000012028 Fenton's reagent Substances 0.000 claims description 2
- VZJVWSHVAAUDKD-UHFFFAOYSA-N Potassium permanganate Chemical compound 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[O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 2
- 239000012286 potassium permanganate Substances 0.000 claims description 2
- 235000019394 potassium persulphate Nutrition 0.000 claims description 2
- 229910052753 mercury Inorganic materials 0.000 abstract description 8
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound 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[Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 abstract description 6
- 239000000126 substances Substances 0.000 abstract description 5
- 239000002244 precipitates Substances 0.000 abstract description 3
- 239000004152 Nitrogen oxides Substances 0.000 abstract 1
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- 239000007795 chemical reaction products Substances 0.000 abstract 1
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- 229910052815 sulfur oxides Inorganic materials 0.000 abstract 1
- 239000003344 environmental pollutants Substances 0.000 description 24
- 231100000719 pollutant Toxicity 0.000 description 24
- 239000000243 solutions Substances 0.000 description 12
- 238000005516 engineering processes Methods 0.000 description 9
- 239000003595 mist Substances 0.000 description 8
- 238000002604 ultrasonography Methods 0.000 description 7
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- 239000000779 smoke Substances 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound 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OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 239000011259 mixed solutions Substances 0.000 description 4
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous Oxide Chemical compound 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[O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 4
- 239000007787 solids Substances 0.000 description 4
- 239000011977 sulfuric acid Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 210000000887 Face Anatomy 0.000 description 2
- 102100011100 Neutral amino acid transporter A Human genes 0.000 description 2
- 101710081281 Neutral amino acid transporter A Proteins 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003054 catalysts Substances 0.000 description 2
- 238000006555 catalytic reactions Methods 0.000 description 2
- 239000002131 composite materials Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229940074994 mercuric sulfate Drugs 0.000 description 2
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- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound 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- 238000003916 acid precipitation Methods 0.000 description 1
- 231100000693 bioaccumulation Toxicity 0.000 description 1
- 230000003197 catalytic Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000356 contaminants Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002349 favourable Effects 0.000 description 1
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- 239000011780 sodium chloride Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000006276 transfer reactions Methods 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
Description
超声波一体化脱硫脱硝脱汞方法及其装置
技术领域
本发明属于大气污染物控制领域,具体涉及一种超声波一体化脱硫脱硝脱荥方法及其 装置。 背景技术
烟气体中的硫氧化物和氮氧化物是形成酸雨和酸雾的主要原因,对生态环境和人体健 康造成了极大的危害,有效治理二者的排放势在必行。燃煤过程排放的汞在局部汞循环中 具有相当大的危害性,其危害不仅具有隐蔽性,而且具有潜在性,即汞的生物累积难于消 除,因此对汞的减排问题同样是国家面临的一项重要问题。目前,烟气污染物的脱除方法 很多,但能够获得实际应用的很少,即使目前获得工业应用的几种污染物控制方法也都具 有各自的不足之处,现归纳如下:
在众多的脱硫方法中,石灰石一石膏湿法烟气脱硫技术以其技术成熟,使用煤种广, 脱硫效率高而获得广泛应用,但该方法具有系统复杂,初始投资和运行费用相对较高,尤 其是如何对反应产物进行有效的处理或利用已经成为该项技术面临的一个难题;
在众多的脱硝方法中,NH3-SCR催化技术因其具有转化率高、选择性好、实用性强等 特点在发达国家得到了广泛的应用,但其过程中会因NH3泄露而造成二次污染问题,而 且,催化剂的损耗导致的运行费用的增加是其目前需要解决的重要问题;
烟气脱Hg技术目前研究较多的活性碳吸附脱除法,但该技术具有成本过高,对Hg01 的吸附脱除效率低等问题而难以获得大规模的工业应用。
此外,对污染物进行分别脱除具有投资和运行费用高、设备复杂和占地面积大等诸多 不足,目前许多烟气污染物同时脱除方法大都是几种方法的简单结合,并非真正的实现同 时脱除,因而,研究开发能够对多种烟气污染物进行一体化脱除的装置及方法是当前的重 要任务之一。 发明内容
为了克服当前的各种烟气污染物控制技术的不足,本发明提供一种超声波一体化脱硫 脱硝脱汞的方法及其装置,主要利用超声波技术产生空化效应,实现烟气中的硫氧化物、 氮氧化物和汞的一体化脱除,该系统具有结构简单,环保经济等优点,具有良好的工业应 用前景。
为实现上述目的,本发明采用的技术方案是: 一种超声波一体化脱硫脱硝脱汞方法, 其特征在于利用超声波在反应液中产生空化效应时释放出的具有强氧化性的羟基自由基 OH、与经过除尘的烟气中的硫氧化物、氮氧化物和Hge发生氧化脱除反应,反应后的洁 净烟气由烟囱排入大气,经分离所得的混合酸液用氨水吸收后制造肥料,而重金属沉淀物 则进行提取回收。
烟气至少经过二级除尘,末级釆用静电除尘;所说反应液为水或包括Fenton试剂、类 Fenton试剂、双氧水、臭氧、高锰酸钾、过硫酸钾在内的氧化剂水溶液。
超声波的有效频率范围为20KHz-500KHz,超声波强度在20W/cm2-80W/cm2;化学反
应在常压下进行,有效反应温度为0'C-8(TC,烟气出口流速在0.005m/s-0.08m/s之间,鼓 泡床反应器内的反应溶液循环流速为0.02 m/s -0.2m/s。
根据上述方法设计的一种超声波一体化脱硫脱硝脱汞装置,其特征在于设有超声波发 生器及其发射器、冷却水系统(包括外置冷却水套和内置冷却盘管)、鼓泡床反应器、静 电除尘器、烟气扩散器、分离塔和止回阀,超声波发射器于鼓泡床反应器内的反应液中, 鼓泡床反应器内外设有冷却水系统,冷却水出口和冷却水入口分别位于冷却水系统的上、 下部,烟气通入管顺序通过静电除尘器和止回阀并由鼓泡床反应器底部接入烟气扩散器, 烟气出口位于鼓泡床反应器上部,鼓泡床反应器底部开有渣垢排泄口,分离塔入口接于鼓 泡床反应器下部的反应产物出口,分离塔的底面、顶部和侧面分别设有反应产物难溶物出 口、药剂投放口和反应产物易溶物出口。其中,进入分离塔内的易溶物主要为硫酸和硝酸 混合溶液,而难溶物主要为硫酸汞沉淀物,主要通过从药剂投放口添加药剂(考虑溶液具 有强酸性,可以选择聚丙烯酰胺絮凝剂系列)促进难溶物沉淀。
所说烟气扩散器采用旋流型喷嘴,强化鼓泡床反应器内扩散和挠动,其布置形式采用 等距和等角的交差排列形式,具体排列密度由旋流喷嘴的旋流角和出口流速以及现场实际 情况确定;
超声波发射器必须保持竖直和悬空状态,超声波布阵方式采用交叉差排列形式,超声 波发射器的有效发射端面必须全部插入反应液液面以下;超声波发生器及发射器可以是变 幅杆式或清洗式;冷却水系统采用外置和内置的双冷却系统,外部为冷却套,内部为冷却 盘管,两者并联;
在安装多部超声波发生器及发射器时,多部要保持发射频率相同、之间要保持等距、 旋转角度相同。
经过一级除尘的烟气经烟道送入静电除尘器,待除去固体颗粒物后经烟气扩散器均匀 扩散至鼓泡床反应器内,超声波发生器将电能转化为声能并通过超声波发射器将声能传递 到溶液中,超声波在溶液中产生空化效应,释放出大量的具有强氧化性的羟基自由基0H-, 与烟气中的硫氧化物、氮氧化物和HgG发生氧化脱除反应,经过处理的洁净烟气由烟囱排 入大气,经分离塔分离所得的混合酸液用氨水吸收后制造肥料,而重金属沉淀物则进行提 取回收。
由于进入鼓泡床反应器的颗粒物容易造成超声波的剧烈衰减,降低超声波能量的利用 效率,因此,进入鼓泡床反应器的烟气必须首先经过静电除尘器除尘,使得进入鼓泡床反 应器的颗粒数量尽可能达到最小化。本方法利用超声波的空化效应产生具有强氧化性的羟 基自由基对烟气污染物进行氧化脱除,利用产生的机械效应强化化学反应的传热传质过 程,加快化学反应速率,提高生产率,实验证明,超声波的有效频率范围为20KHZ-500 KHz 之间,频率太低或太高均会导致空化效应变得不明显或者无空化效应,超声波最佳强度在 20W/cm2-80W/cm2之间,超声强度太小,空化效应不明显,污染物脱除效率不高,难以 满足环保要求,而强度过高则会因为声屏蔽现象导致超声波的声能利用率大幅度下降,增 加了经济成本。
鼓泡床反应器内的化学反应在常压下进行,这既降低了对鼓泡床反应器材料的要求, 也提高了反应的安全可靠性,省去了许多高压反应加压所带来的耗能难题。有效反应温度 为0°C-80°C,免去了氮氧化物在选择性催化脱除时加热升温所引发的能耗的问题,反应 在室温度下即可以进行,温度可以通过冷却水系统进行调节和控制。烟气出口流速在 0.005m/s-0.08m/s之间,溶液循环流速为0.02 m/s-0.2m/s,烟气出口流速和循环液流速太 低则不利于气液反应的传质-反应过程,但速度过高则气液接触时间縮短,而空化泡的形 成需要时间,因此速度太高则不利于空化泡的形成。本系统对不同成分的混合气体和高低 浓度的污染物气体的处理均具有良好的效果,具有适用范围广泛等优点。
本发明可以对烟气中的硫氧化物、氮氧化物和Hge进行一体化脱除,对其中一种、两 种甚至多种污染物单独或者同时脱除都适用,这在当前的各种烟气污染物脱除方法中是不 多见的,这可以大幅度节省初试投资成本和运行维护费用,具有良好的应用前景。
烟气扩散盘是关键部件,采用旋流型喷嘴强化鼓泡床反应器内扩散和挠动,加强化学 反应的传热传质速率,采用等距和等角的交差排列形式,具体数量由旋流喷嘴的旋流角度 和出口流速以及现场实际情况确定。反应器采用烟气处理量较大的鼓泡床反应器,超声波 发生器及发射器可以是变幅杆式和清洗式,在安装多部超声波发生器及发射器时,多部要 保持发射频率相同,发射器之间要保持等距,间距同为a,旋转角度同为B,距离和角度具 体大小结合所处理烟气的相关性质和现场情况统筹确定,超声波发射器必须保持竖直和悬 空状态,超声波布阵方式采用差排,有效发射端面必须全部插入液面以下,充分利用声能, 提高节能效果。
另外,由于溶液中颗粒物引起声波的反射和散射现象,会造成声波急剧的衰减,降低 声能的利用效率,因此,烟气在进入烟气扩散器前必须要经过二级以上除尘,第一级可由 普通的除尘器除去大中径固体颗粒,末级则必须采用静电除尘器除去微小颗粒。此外,由 于超声波的空化效应对温度的变化极为敏感,实验研究表明,温度过高不利于空化效应的 产生,同时气体的溶解度也会下降,削弱了气液传质-反应的进行,但若在内部设置过多 的冷却盘管则势必占据过多的反应空间,其次还会造成声波衰减,降低声能的利用率,采 用内外置复合冷却系统并联结合的方式可以有效减少内设盘管的压力,还可以对内外系统 进行流量调节来控制反应器内部温度的大小和均匀度。 本发明的优点及有益效果:
目前采用的各种脱硫、脱硝、脱汞方法均具有各自的不足,例如石灰石一石膏湿法烟 气脱硫技术具有系统复杂,初始投资和运行费用相对较高,以及反应产物难以获得有效的 处理或利用等不足;而NH3-SCR催化技术具有NH3泄露而造成二次污染问题,运行中催 化剂的损耗导致的运行费用的增加是其目前需要解决的重要问题;烟气脱汞技术目前研究 较多的活性碳吸附脱除法具有成本过高,对Hgn的吸附脱除效率低等不足;此外,对污染 物进行分别脱除具有投资和运行费用高、设备复杂和占地面积大等诸多不足,本发明具备 以下的诸多优点能够有效解决上面的问题。
本发明中,烟气由经静电除尘器和止回阀通入烟气扩散器,随后均匀扩散至鼓泡床反 应器内,与超声波空化效应产生的大量的具有强氧化性的羟基自由基(OH0发生氧化脱
除反应,羟基自由基(OH*)能有效地将烟气中的难溶物S02、 NO和HgG分别氧化为易容 于水的S03、 NO^nHg2+ , S03和N02溶于水后形成H2S04和HN03混合溶液,而Hg2+和 硫酸反应能生成难溶物Hg2S04沉淀下来,有利于化学反应平衡右移,从而进一步提高化 学反应的进行,进而达到多种污染物同时脱除的目的,反应后的混合酸液和重金属盐沉淀 物进入分离塔后进行适当的粗分离后即可用于制取制造化肥等,而重金属沉淀物则可以进 行提取回收,整个过程无二次污染,是一种高效、环保、经济的新型烟气污染物一体化脱 除方法。
其基本原理如下:
超声波空化效应:
H20 — H + OH •H + *H — H2 •OH + -OH — H202
脱硫反应机理:
S02 + OH — HS03 HS03+.OH — H2S04 总反应式:S02+H2S04
脱硝反应机理:
NO+OH—HN02
HN02+ .OH —N02+ H20
NO+.OH—N02+ H-
2N02+ H20 — HN02 + HN03
总反应式:NO + 3.0H—HN03 + H20
脱汞反应机理:
Hg0 + 2.0H —Hg2+ + 20H-Hg2++S042+—HgS04(i) —OH+ H+—H20 总反应式:HgQ + 2'OH +H2S04 — Hg S04 (丄)+ 2H20
本发明可以对烟气中的硫氧化物、氮氧化物和Hg^进行一体化脱除,对其中一种、两 种或者多种污染物脱除都适用,这在当前的各种脱出方法中是不多见的,可以大幅度节省 初试投资成本和运行维护费用。而且适用范围广泛,具有初始投资和运行费用少,结构简 单,操作方便,占地面积小等诸多优点,是一种具有广泛应用前景的烟气污染物控制方法 及装置。 附图说明
图1是本发明的硬件总体结构图; 图2是超声波发射器的布阵形式局部图; 图3是扩散器的旋流喷嘴布阵形式局部图。 具体实施方式 下面结合附图及实施例对本发明的工作原理及工作过程作进一步说明。
参看图l,本发明的超声波一体化脱硫脱硝脱汞装置主要由超声波发生器8、超声波 发射器l、冷却水系统(包括冷却水套和冷却盘管)2、鼓泡床反应器3、静电除尘器4、 烟气扩散器5、分离塔6和止回阔7等组成;超声波发射器l置于鼓泡床反应器3内的反 应液中,鼓泡床反应器3内外设有冷却水系统2,冷却水出口 (G)和冷却水入口 (F) 分别位于鼓泡床反应器3的上、下部,由一级除尘器处理后的烟气A顺序通过静电除尘 器4和止回阀7并由鼓泡床反应器3底部接入烟气扩散器5,烟气出口 (B)位于鼓泡床 反应器3上部,鼓泡床反应器3底部开有渣垢排泄口 (E),分离塔6入口 (H)接于鼓泡 床反应器3下部的反应产物出口 (D),分离塔6于底部、顶部和侧面分别设有反应产物 难溶物出口 (J)、药剂投放口 (K)和反应产物易溶物出口 (1), C为反应液添加口。
参看图2和3,在安装多部超声波发生器及发射器时,多部要保持发射频率相同,之 间要保持等距,其具体布置形式如图2所示,间距同为a,旋转角度同为B,距离和角度具 体大小结合操作条件以及所处理烟气的相关性质和现场情况统筹确定。超声波发射器必须 保持竖直和悬空状态,超声波布阵方式采用交差排列,有效发射端面必须全部插入反应液 液面9以下,充分利用声能,提高节能效果。系统中的烟气扩散器是关键部件,采用旋流 型喷嘴强化反应器内扩散和挠动,加强化学反应的传热传质速率,其布置形式如附图3 所示,采用等距和等角的交差排列形式,具体数量由购买的旋流喷嘴的旋流角度和出口流 速以及现场实际情况确定。
由于反应液中颗粒物会造成声波的反射和散射,会造成声波急剧的衰减,降低声能的 利用效率,因此,烟气在进入烟气扩散器前必须要经过二级以上除尘,第一级可由普通除 尘器除去大中径固体颗粒,第二级则必须采用静电除尘器除去微小颗粒。反应器采用烟气 处理量较大的鼓泡床反应器,超声波装置可以是变幅杆式和清洗式。此外,由于超声波的 空化效应对温度的变化极为敏感,实验研究表明,温度过高不利于空化效应的产生,同时 气体的溶解度也会下降,若在内部设置过多的冷却盘管则势必占据过多的反应空间,其次 还会造成声波衰减,降低声波的利用率,采用内外置复合冷却系统结合的方式可以有效减 少内设盘管的压力,还可以对内外系统进行流量调节来控制反应器内部温度的大小和均匀 度,其中内置盘管的设置量可以根据烟气处理量好具体装置的结构形式来确定。
经一级除尘的烟气经烟道由A处送入静电除尘器4,待除去固体颗粒物后经烟气扩散器 5均匀扩散至鼓泡床反应器3内,超声波发生器8将电能转化为声能并通过超声波发射器1 将声能传递到反应液中,超声波在反应液中产生空化效应,时释放出大量的具有强氧化性 的羟基自由基OH、与烟气中的硫氧化物、氮氧化物和Hga发生氧化脱除反应,能有效地 将烟气中的难溶物S02、 NO和Hg0分别氧化为易容于水的S03、 N02和Hg^ ,SO^PN02 溶于水后形成H2S04和HN03混合溶液,而Hg^和硫酸反应能生成难溶物Hg2S04沉淀下来, 有利于化学反应平衡右移,从而进一步提高化学反应的进行,进而达到多种污染物同时脱 除的目的。经过处理的烟气经B处排出,产生的渣垢由E处排出,反应产物则由B处进入分 离塔6,在分离塔6内稍作分离后即可用氨水吸收后制造化肥等,而重金属沉淀物则可以进 行提取回收,整个过程无二次污染,是一种高效、环保和经济的烟气污染物一体化脱除装
置及方法。
其中,进入分离塔内的易溶物主要为硫酸和硝酸混合溶液,而难溶物主要为硫酸汞沉淀 物,主要通过从药剂投放口添加药剂(考虑溶液具有强酸性,可以选择聚丙烯酰胺絮凝剂 系列)促进难溶物沉淀。
下面是几组具体实际应用时的操作参数和脱除效果: 第一组: 主要操作参数-
<table>table see original document page 8</column></row> <table>第二组: 主要操作参数:
<table>table see original document page 8</column></row> <table>
第三组: 主要操作参数:<table>table see original document page 9</column></row> <table>第四组: 主要操作参数:<table>table see original document page 9</column></row> <table>第五组: 主要操作参数-<table>table see original document page 9</column></row> <table>
脱除效率
<table>table see original document page 10</column></row> <table>第六组-主要操作参数:
<table>table see original document page 10</column></row> <table>脱除效率
<table>table see original document page 10</column></row> <table>可见,超声波声强度,反应温度,声波频率,出口浓度和气流流速等因素对污染物的脱 除效率均有重要的影响,具体应用时应根据实际情况选择最佳操作参数。
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