CN202289835U - 有机废气净化系统 - Google Patents
有机废气净化系统 Download PDFInfo
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- CN202289835U CN202289835U CN2011204186919U CN201120418691U CN202289835U CN 202289835 U CN202289835 U CN 202289835U CN 2011204186919 U CN2011204186919 U CN 2011204186919U CN 201120418691 U CN201120418691 U CN 201120418691U CN 202289835 U CN202289835 U CN 202289835U
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- Prior art keywords
- organic waste
- communicated
- gas purification
- photocatalytic reaction
- gas
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- 239000007789 gases Substances 0.000 title claims abstract description 22
- 239000010815 organic wastes Substances 0.000 title abstract description 12
- 238000000746 purification Methods 0.000 claims abstract description 40
- 239000003921 oils Substances 0.000 claims abstract description 14
- 239000002912 waste gases Substances 0.000 claims description 30
- 238000006243 chemical reactions Methods 0.000 claims description 26
- 230000001699 photocatalysis Effects 0.000 claims description 26
- 239000000428 dust Substances 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 12
- 239000003054 catalysts Substances 0.000 claims description 10
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 4
- 239000004917 carbon fibers Substances 0.000 claims description 4
- 238000007084 catalytic combustion reactions Methods 0.000 claims description 4
- 239000003365 glass fibers Substances 0.000 claims description 4
- 238000006555 catalytic reactions Methods 0.000 abstract description 11
- 239000002245 particles Substances 0.000 abstract description 9
- 239000000126 substances Substances 0.000 abstract description 4
- 239000003595 mist Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound 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C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 2
- 239000011892 benzene Substances 0.000 abstract 2
- 238000006065 biodegradation reactions Methods 0.000 abstract 1
- 150000003384 small molecules Chemical class 0.000 abstract 1
- 125000001997 phenyl group Chemical group 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- 239000011135 tin Substances 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound 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O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 229910000504 titanium dioxide Inorganic materials 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
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Abstract
本实用新型适用于有机废气处理技术领域，提供了一种有机废气净化系统，包括依次连通的预处理装置及光催化反应装置，其特征在于，该有机废气净化系统还包括生物净化装置，该光催化反应装置与该生物净化装置依次连通。本实用新型有机废气净化系统，通过将预处理，将有机废气中粒径大于2.5微米的颗粒物去除，将油雾、大颗粒物质分离，通过光催化反应，将有机废气中生物难降解的苯环类的物质经过紫外光先分解成小分子或将苯环类经紫外光裂解，从而大幅度地提高苯环类物质的生物可降解性；通过生物净化处理，实现了有机废气净化效果进一步提升。
Description
有机废气净化系统
技术领域
[0001] 本实用新型属于废气处理技术领域，尤其涉及一种有机废气净化系统。 背景技术
[0002] 挥发性有机废气是仅次于颗粒物污染废气、ニ氧化硫和氮氧化物废气的有一大类大气污染源，对环境危害大，目前我国大气污染物综合排放标准（GB16^7-1996)对其中含 14类挥发性有机污染物的废气规定了最高允许排放浓度。挥发性有机废气净化方法有多种，如：燃烧法、吸收法、吸附法、冷凝法等。低浓度挥发性有机废气，由于量大，浓度低，采用上述常规的化学或物理方法难以达到经济，有效的处理目的，还会产生二次污染问题，因此低浓度挥发性有机废气污染治理是我国同时也是世界范围内挥发性有机废气净化领域的一大难题。
实用新型内容
[0003] 有鉴于此，本实用新型提供一种有机废气净化系统，解决现有技术中有机废气处理污染大、成本高的技术问题。
[0004] 本实用新型是这样实现的，
[0005] 一种有机废气净化系统，包括依次连通的预处理装置及光催化反应装置，还包括生物浄化装置，所述光催化反应装置与所述生物浄化装置依次连通。
[0006] 进一歩，所述预处理装置包括依次连通的除尘装置和油雾分离装置，所述油雾分离装置与光催化反应装置连通。
[0007] 进一歩，所述预处理装置包括互相连通的除尘装置和油雾分离装置，所述除尘装置与光催化反应装置连通。
[0008] 进一歩，所述除尘装置为袋式除尘器。
[0009] 进一歩，所述有机废气净化系统还包括冷却装置，所述冷却装置与所述预处理装置依次连通。
[0010] 进一歩，所述冷却装置与所述除尘装置连通。
[0011] 进一歩，所述光催化反应装置的光源组件为紫外光光源组件。
[0012] 进一歩，所述光催化反应装置内设有催化剂固定组件。
[0013] 进一歩，所述催化剂固定组件为玻璃纤维网。
[0014] 进一歩，所述生物浄化装置内设有互相连通的生物膜填料塔和活性炭纤维吸附组件，所述生物膜填料塔与光催化反应装置连通。
[0015] 本实用新型有机废气净化系统，通过将预处理，将有机废气中粒径大于2. 5微米的颗粒物去除，将油雾、大颗粒物质分离，通过光催化反应，将有机废气中生物难降解的苯环类的物质经过紫外光先分解成小分子或将苯环类经紫外光裂解，从而大幅度地提高苯环类物质的生物可降解性；通过生物浄化处理，实现了有机废气净化效果进ー步提升。附图说明[0016]图I是本实用新型实施例有机废气净化系统结构图。具体实施方式[0017] 为了使本实用新型的目的、技术方案及优点更加清楚明白，以下结合附图及实施例，对本实用新型进行进一步详细说明。应当理解，此处所描述的具体实施例仅仅用以解释本实用新型，并不用于限定本实用新型。[0018] 请参阅图I,图I显示本实用新型实施例有机废气净化系统结构图，包括依次连通的预处理装置I及光催化反应装置2，该有机废气净化系统还包括生物净化装置3，该光催化反应装置2与该生物净化装置3依次连通。[0019]本实用新型实施例中，该有机废气是指（各类工业废气，特别为苯系类芳香族化合物。该有机废气经过该有机废气净化系统的进气口进入有机废气净化系统中进行净化处理。[0020] 具体地，本实用新型实施例有机废气净化系统，包括预处理装置I和光催化反应装置2，该预处理装置I要和光催化反应装置2依次连接，该有机废气净化系统还包括生物净化装置3，该光催化反应装置2与该生物净化装置3依次连通；即待处理的有机废气进入至本实用新型实施例有机废气净化系统后，进过预处理装置I预处理后，再进入光催化反应装置2进行光催化反应，有机废气经过光催化反应后，进入生物进化装置3中进行生物净化。[0021] 具体地，该预处理装置I包括相通连接的除尘装置11和油雾分离装置12，该除尘装置11和油雾分离装置12的设置没有顺序要求，可以先设置除尘装置11，则该油雾分离装置12与光催化反应装置2连通；也可以先设置油雾分离装置12，则该除尘装置11与光催化反应装置2连通。该除尘装置11为袋式除尘器；通过设置除尘装置11和油雾分离装置12，将有机废气中粒径大于2. 5微米的颗粒物去除，将油雾、大颗粒物质分离，使有机废气更有利于后续的光催化反应和生物净化。[0022] 进一步地，该有机废气净化系统还包括冷却装置4，该冷却装置4与该预处理装置 I依次连接，即该冷却装置4设置于该预处理装置I之前。具体地，所述冷却装置4与所述除尘装置11连通。待处理的有机废气经过冷却装置4的冷却处理后，进入至预处理装置I 中进行预处理。通过设置设置冷却装置4，使得待处理的有机废气温度大大降低，一方面减少了对设备的损害，同时，保证了后续生物进化装置3中微生物存活，不会因为待处理有机废气的高温死亡。[0023] 具体地，该光催化反应装置2包括催化剂固定组件；该催化剂固定组件为玻璃纤维，该玻璃纤维上附着有光催化反应催化剂。该光催化反应催化剂选自纳米级氧化锌/二氧化锡复合物或二氧化钛，该光催化反应装置的光源组件为紫外光光源组件。待处理有机废气进入光催化反应装置2后，以紫外光为光源，以氧化锌/ 二氧化锡复合物或二氧化钛为催化剂，进行光催化分解反应，将有机废气中生物难降解的苯环类的物质经过紫外光先分解成小分子或将苯环类经紫外光裂解，从而大幅度地提高苯环类物质的生物可降解性；通过选用上述粒径范围的催化剂，使得更多的催化剂能够附着在催化剂固定装置上，使得有机废气的光催化反应进行更加彻底。[0024] 具体地，该生物净化装置3内设有相互连通的生物膜填料塔31和活性炭纤维吸附组件32 ;该生物膜填料塔31中分布有进行生物净化处理的微生物例如菌种B350。经过光催化反应处理后的有机废气进入该生物膜填料塔中，由该生物膜填料塔中的微生物进行进一步降解，使有机废气中的有机物含量大大降低。[0025] 有机废气经过生物膜填料塔31的生物净化处理后，进入活性炭纤维吸附组件32 中，利用活性炭纤维的高吸附特点，将有机废气中的杂质吸附，去除，实现有机废气彻底净化，达到排放标准。[0026] 以上所述仅为本实用新型的较佳实施例而已，并不用以限制本实用新型，凡在本实用新型的精神和原则之内所作的任何修改、等同替换和改进等，均应包含在本实用新型的保护范围之内。
Claims (10)
1. 一种有机废气净化系统，包括依次连通的预处理装置及光催化反应装置，其特征在于，还包括生物净化装置，所述光催化反应装置与所述生物净化装置依次连通。
2.如权利要求I所述的有机废气净化系统，其特征在于，所述预处理装置包括互相连通的除尘装置和油雾分离装置，所述油雾分离装置与光催化反应装置连通。
3.如权利要求I所述的有机废气净化系统，其特征在于，所述预处理装置包括互相连通的除尘装置和油雾分离装置，所述除尘装置与光催化反应装置连通。
4.如权利要求2或3所述的有机废气净化系统，其特征在于，所述除尘装置为袋式除尘器。
5.如权利要求2或3所述的有机废气净化系统，其特征在于，还包括冷却装置，所述冷却装置与所述预处理装置依次连通。
6.如权利要求5所述的有机废气净化系统，其特征在于，所述冷却装置与所述除尘装置连通。
7.如权利要求I所述的有机废气净化系统，其特征在于，所述光催化反应装置的光源组件为紫外光光源组件。
8.如权利要求I所述的有机废气净化系统，其特征在于，所述光催化反应装置内设有催化剂固定组件。
9.如权利要求I所述的有机废气净化系统，其特征在于，所述催化剂固定组件为玻璃纤维网。
10.如权利要求I所述的有机废气净化系统，其特征在于，所述生物净化装置内设有互相连通的生物膜填料塔和活性炭纤维吸附组件，所述生物膜填料塔与光催化反应装置连通。
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| CN103172111A (zh) * | 2013-03-14 | 2013-06-26 | 中国科学院广州地球化学研究所 | 有机杂气纯化装置和纯化方法 |
| CN103721510A (zh) * | 2013-12-13 | 2014-04-16 | 江苏中科睿赛污染控制工程有限公司 | 一种VOCs高效处理方法 |
| CN105169927A (zh) * | 2015-10-14 | 2015-12-23 | 安徽省绿巨人环境技术有限公司 | 有机废气处理装置及方法 |
| CN105363342A (zh) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | 一种处理有机废气的方法 |
| CN105771506A (zh) * | 2016-03-08 | 2016-07-20 | 张文国 | 一种工业垃圾裂化焚烧尾气除尘处理系统 |
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| CN107837660A (zh) * | 2017-10-24 | 2018-03-27 | 宁波华九文化传媒有限公司 | 带废热回收利用的工业废气净化处理装置 |
| CN110170225A (zh) * | 2019-06-03 | 2019-08-27 | 南京瑞轩环保科技有限公司 | 一种节能环保的胶合板生产废气的处理方法 |
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| CN103172111A (zh) * | 2013-03-14 | 2013-06-26 | 中国科学院广州地球化学研究所 | 有机杂气纯化装置和纯化方法 |
| CN103172111B (zh) * | 2013-03-14 | 2015-12-09 | 中国科学院广州地球化学研究所 | 有机杂气纯化装置和纯化方法 |
| CN103721510A (zh) * | 2013-12-13 | 2014-04-16 | 江苏中科睿赛污染控制工程有限公司 | 一种VOCs高效处理方法 |
| CN105363342A (zh) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | 一种处理有机废气的方法 |
| CN105169927A (zh) * | 2015-10-14 | 2015-12-23 | 安徽省绿巨人环境技术有限公司 | 有机废气处理装置及方法 |
| CN105771506A (zh) * | 2016-03-08 | 2016-07-20 | 张文国 | 一种工业垃圾裂化焚烧尾气除尘处理系统 |
| CN106178875A (zh) * | 2016-08-16 | 2016-12-07 | 南京格洛特环境工程股份有限公司 | 一种紫外灯强化处理挥发性有机废气的工艺 |
| CN107837660A (zh) * | 2017-10-24 | 2018-03-27 | 宁波华九文化传媒有限公司 | 带废热回收利用的工业废气净化处理装置 |
| CN110170225A (zh) * | 2019-06-03 | 2019-08-27 | 南京瑞轩环保科技有限公司 | 一种节能环保的胶合板生产废气的处理方法 |
| CN110170225B (zh) * | 2019-06-03 | 2020-02-28 | 南京瑞轩环保科技有限公司 | 一种节能环保的胶合板生产废气的处理方法 |
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