CN203853005U - VOCs废气净化装置 - Google Patents
VOCs废气净化装置 Download PDFInfo
- Publication number
- CN203853005U CN203853005U CN201320780197.6U CN201320780197U CN203853005U CN 203853005 U CN203853005 U CN 203853005U CN 201320780197 U CN201320780197 U CN 201320780197U CN 203853005 U CN203853005 U CN 203853005U
- Authority
- CN
- China
- Prior art keywords
- waste gas
- vocs waste
- vocs
- temperature plasma
- low
- Prior art date
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- 239000002912 waste gases Substances 0.000 title claims abstract description 80
- 238000000746 purification Methods 0.000 title claims abstract description 22
- 150000002894 organic compounds Chemical class 0.000 title abstract 5
- 210000002381 Plasma Anatomy 0.000 claims abstract description 27
- 238000010521 absorption reactions Methods 0.000 claims abstract description 25
- 239000007789 gases Substances 0.000 claims abstract description 22
- 239000003513 alkali Substances 0.000 claims abstract description 18
- 239000000463 materials Substances 0.000 claims abstract description 7
- 230000002378 acidificating Effects 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 238000003379 elimination reactions Methods 0.000 claims description 2
- 238000000034 methods Methods 0.000 abstract description 18
- 239000003570 air Substances 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract description 4
- 239000007788 liquids Substances 0.000 abstract 4
- 238000007789 sealing Methods 0.000 abstract 1
- 239000002699 waste materials Substances 0.000 abstract 1
- 238000005516 engineering processes Methods 0.000 description 6
- 239000003897 fog Substances 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005868 electrolysis reactions Methods 0.000 description 4
- 239000011901 water Substances 0.000 description 4
- 238000005336 cracking Methods 0.000 description 3
- 238000005474 detonation Methods 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nODVweCcgaGVpZ2h0PSc4NXB4JyB2aWV3Qm94PScwIDAgODUgODUnPgo8IS0tIEVORCBPRiBIRUFERVIgLS0+CjxyZWN0IHN0eWxlPSdvcGFjaXR5OjEuMDtmaWxsOiNGRkZGRkY7c3Ryb2tlOm5vbmUnIHdpZHRoPSc4NScgaGVpZ2h0PSc4NScgeD0nMCcgeT0nMCc+IDwvcmVjdD4KPHRleHQgZG9taW5hbnQtYmFzZWxpbmU9ImNlbnRyYWwiIHRleHQtYW5jaG9yPSJlbmQiIHg9JzU3Ljc5NzInIHk9JzQ3LjMxMDQnIHN0eWxlPSdmb250LXNpemU6MzJweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjtmaWxsOiNGQ0M2MzMnID48dHNwYW4+SDwvdHNwYW4+PHRzcGFuIHN0eWxlPSdiYXNlbGluZS1zaGlmdDpzdWI7Zm9udC1zaXplOjI0cHg7Jz4yPC90c3Bhbj48dHNwYW4+UzwvdHNwYW4+PC90ZXh0Pgo8L3N2Zz4K S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 230000035943 smell Effects 0.000 description 2
- 239000000126 substances Substances 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 206010022114 Injuries Diseases 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229930012076 Naphthalene Natural products 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 238000010504 bond cleavage reactions Methods 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound 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O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxides Inorganic materials 0.000 description 1
- 239000003054 catalysts Substances 0.000 description 1
- 210000004027 cells Anatomy 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- 239000003814 drugs Substances 0.000 description 1
- 239000000796 flavoring agents Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene Chemical compound 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C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000002245 particles Substances 0.000 description 1
- 125000001997 phenyl group Chemical class 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[H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000012047 saturated solutions Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000004083 survival Effects 0.000 description 1
- 238000004065 wastewater treatment 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
技术领域
[0001] 本实用新型涉及一种废物处理净化装置,尤其涉及一种VOCs废气净化装置。
背景技术
[0002] 在工业企业的废水处理和市政行业的污水处理、垃圾中转站及填埋过程中,会产生含有大量挥发性有机物(VOCs)的异味气体,VOCs废气成极复杂,常见的有烃类、醛类、苯类、氯代烃类、萘、二异氰酸酯类等,多有恶臭气味,表现出程度不同的毒性、刺激性,而且有些化合物有基因性毒性,对周围动植物及人类生存环境造成较大影响,因此对VOCS废气的净化对环境保护而言就极为重要了,常规的VOCs废气净化方法包括电解法、触媒焚化法、活性碳吸附法、吸收法、冷凝法、生物法等。中国实用新型专利CN102814110A公开了一种除异味、降解VOCs净化装置,该装置包括一个进风口通道;至少一个内设有除雾折板的除雾箱,该除雾箱同入口通道连通;一个内设有可放电的线筒式低温等离子箱,该低温等离子箱同除雾箱连通;一个出风口通道,该出风口通道同低温等离子箱连通。从进风口进入的含有恶臭以及挥发性有机物(VOCs)的废气首先到达泄压箱,随后废气到达除雾箱,而后到达低温等离子箱。净化后的气体通过出口段向上流动,由出风口达标排放。但是采用这种技术,无法将VOCs废气中的物质包括有机物、酸性物质等彻底清除干净,并且从除雾箱排出后排至低温等离子箱时,未将酸性物质清除,在与低温等离子反应时会容易引起爆鸣,存在安全隐患,并且对设备会造成一定伤害。
[0003] 中国发明专利CN102895851A公开了一种VOCs双解处理方法,该方法包括电解工艺段步骤及分子裂解工艺段步骤,在电解工艺段步骤中,连续导入含VOCs气体并同时连续喷淋水,从而分离可溶性VOCs和不溶性VOCs,其中可溶性VOCs形成饱和溶液,并通过在电解槽中形成的正负电荷在正负电极周围吸附连续形成絮凝物;对从所述电解工艺段步骤中分离出的不溶性VOCs及逸出的可溶性VOCs,进行所述分子裂解工艺段步骤,在该分子裂解工艺段步骤中,高压窄脉冲放电作用于VOCs分子,将大部分VOCs分子中的化学键断键裂解为水和二氧化碳,部分VOCs转化为有机酸或无机酸。实现了 VOCs的高效、清洁化去除。但是采用该技术,虽然能够将VOCs比较彻底地去除,但是在工艺过程中要采用多种化学药齐U,需要消耗较多能源,而且结构复杂,成本偏高。
实用新型内容
[0004] 为解决现有技术中存在的不足,本实用新型提供了一种结构简单,并能够有效吸收VOCs废气的VOCs废气净化装置。
[0005] 为实现上述目的,本实用新型的VOCs废气净化装置,包括对VOCs废气进行密闭收集的集气装置,对集气装置内VOCs废气中的酸性物质进行吸收的碱液吸收塔,消除由碱液吸收塔导出的VOCs废气中有机物的低温等离子净化装置,以及为VOCs废气的流通提供动力及排出通道的引风装置。采用上述技术方案,先通过碱液吸收塔对由集气装置导入的VOCs废气进行脱酸处理,然后导入低温等离子净化装置对有机物进行清除,在此过程中由引风装置为VOCs废气提供流通动力,以及在清除完毕后将已经清理干净的气体排出的排出通道。并且VOCs废气浓度太高会导致低温等离子在放电过程中的爆鸣,首先采用碱液吸收可以减少废气中硫化氢等易于水吸收部分有机污染物。
[0006] 作为对上述方式的限定,还包括设置在碱液吸收塔与低温等离子净化装置之间、对VOCs废气进行干燥处理的脱水塔。设置脱水塔,将VOCs废气在进入低温等离子净化装置之前先干燥,除去VOCs废气中的水滴,更加有利于后续的低温等离子对VOCs废气的处理,避免造成不良影响,增长设备的使用寿命。
[0007] 作为对上述方式的限定,还包括对由低温等离子净化装置排出的VOCs废气进行过滤处理的过滤装置。设置过滤装置,将由低温等离子净化装置排出处理过后的VOCs废气中的废物再次吸附,确保VOCs废气被处理干净。
[0008] 作为对上述方式的限定,所述的引风装置包括为VOCs废气净化装置提供全负压环境并为VOCs废气的流通提供动力的引风机,以及将过滤完毕的VOCs废气排出的烟囱。设置引风机,确保VOCs废气在该装置中沿装置的设置方向流通,提供流通动力,并保证了整个装置处于全负压形式,在装置运行时VOCs废气不会泄露,使VOCs废气经过整个流程达到最佳的处理效果;设置烟囱是为处理完毕后的VOCs废气提供排出通道。
[0009] 综上所述,采用上述技术方案,先通过集气装置将VOCs废气密闭收集,再借由引风机提供的流通动力,经过碱液吸收塔的脱酸处理及脱水塔的脱水处理,导入到低温等离子净化装置进行处理,最终过滤后由烟®排出。该装置能够对VOCs废气理想地处理并且能满足排放标准要求,并且针对于VOCs废气浓度太高会导致低温等离子在放电过程中的爆鸣的问题,首先采用碱液吸收可以减少废气中硫化氢等易于水吸收部分有机污染物,同时降低了 VOCs废气浓度,消除了安全隐患。同时引风机为VOCs废气在该装置中沿装置的设置方向流通,提供流通动力,同时保证了整个装置处于全负压形式,在装置运行时VOCs废气不会泄露,使VOCs废气经过整个流程达到最佳的处理效果,投资省、运行成本低,延长仪器的使用寿命,可以极大的提高工作效率,具有广泛的适用性。
附图说明
[0010] 下面结合附图及具体实施方式对本实用新型作更进一步详细说明:
[0011] 图1为本实用新型的结构示意图。
[0012] 图中:
[0013] 1、集气装置;2、碱液吸收塔;3、脱水塔;4、低温等离子净化装置;5、过滤装置;6、引风装置;61、引风机;62、烟囱。
具体实施方式
[0014] 如图1所示,本实施例涉及一种VOCs废气净化装置,包括对VOCs废气进行密闭收集的集气装置1,集气装置I可采用内表面附有防腐蚀材料的气体收集器等装置;与集气装置I连通对VOCs废气中的酸性物质进行吸收的碱液吸收塔2 ;与碱液吸收塔2连通对脱酸处理完毕后的VOCs废气进行干燥处理的脱水塔3 ;与脱水塔3连通将干燥处理后的VOCs废气中有机物消除的低温等离子净化装置4 ;对由低温等离子净化装置4排出的VOCs废气进行过滤处理的过滤装置5,过滤装置5可采用内部设置有对水分、颗粒等气体杂质具有吸附作用的过滤器等;以及为VOCs废气在整个装置中的流通提供动力及排出通道的引风装置
6。引风装置6包括为VOCs废气净化装置提供全负压环境并为VOCs废气的定向流通提供动力的引风机61,以及将过滤完毕的VOCs废气排出的烟囱62。引风机61设置在图中所示的右端,为VOCs废气在沿装置的设置方向即由左往右的流通提供流通动力,并保证了整个装置处于全负压形式,在运行时VOCs废气不会泄露,使VOCs废气经过整个流程达到最佳的处理效果。
[0015] 在利用VOCs废气净化装置进行废气吸收时,先利用集气装置I将VOCs废气密闭收集,再导入到碱液吸收塔2中进行脱酸处理,再导入到脱水塔3中进行干燥处理,再将VOCs废气导入到低温等离子净化装置4中消除有机物,再导入到过滤装置5中确保将废气中遗漏的废物吸附干净,最终由烟囱62排出。在装置的整个工作过程中,由引风机61为VOCs废气的流通提供动力,并且使得整个装置处于全负压形式,避免在运行过程中气体泄漏,确保对于VOCs废气的吸收处理达到最佳效果。
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