CN204619702U - 一种含低浓度voc废气的净化装置 - Google Patents
一种含低浓度voc废气的净化装置 Download PDFInfo
- Publication number
- CN204619702U CN204619702U CN201520240764.8U CN201520240764U CN204619702U CN 204619702 U CN204619702 U CN 204619702U CN 201520240764 U CN201520240764 U CN 201520240764U CN 204619702 U CN204619702 U CN 204619702U
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- Prior art keywords
- desorption
- waste gas
- voc
- activated carbon
- carbon powder
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- 239000002912 waste gas Substances 0.000 title claims abstract description 41
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Classifications
-
- 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
本实用新型涉及一种含低浓度VOC废气的净化装置，包括文丘里气固混合器、高效脉冲袋式除尘器、氧化塔、脱附装置、活性炭粉储罐、小型蓄热氧化炉、热交换器、涤气器、风机；本实用新型文丘里气固混合器混匀炭粉和废气，高效脉冲袋式除尘器将吸附有VOC的炭粉与被吸附了VOC后的废气分离捕集，分离的废气由氧化塔处理，捕集的炭粉由脱附装置脱附，脱附后的炭粉输送至文丘里气固混合器回用，脱附后的VOC由小型蓄热氧化炉分解，热交换器回收热能。本实用新型结构简单、企业可接受性强，适用于含低浓度VOC废气的处理，炭粉和热能的回用降低了成本、避免了中间态污染物的排放，氧化塔、小型蓄热氧化炉使得去除效率极大提高。
Description
技术领域
[0001 ] 本实用新型涉及一种净化装置，特别涉及一种含低浓度VOC废气的净化装置。
背景技术
[0002] 在石油加工、化学合成、油漆制造、喷漆、印刷、合成板材、涂层、电子产品清洗等行业的生产中经常排放挥发性有机物(volatile organic compounds, VOC)，VOC种类繁多，主要包括烃类、醇类、醚类、醛类、酚类、脂类、脂肪酸类、胺类以及有机卤系衍生物等，具有污染面广、有毒、有恶臭、排放量大、浓度低的特点。
[0003] 含低浓度VOC废气的治理方法在作为选择时要根据气体的性质、处理量、当地环境卫生要求和经济情况等具体情况而定。常见的含低浓度VOC废气治理方法有:燃烧法、吸附法、等离子法、光分解法等。燃烧法是通过燃烧把废气中有害可燃组分经氧化生成0)2和H20，主要装置有:燃烧器、燃烧室。该方法去除率高、设备简单，但能耗大，投资和运行费用高。吸附法是利用多孔性材料对含VOC的废气进行吸附处理，从而达到消除有害物的目的；主要装置有预处理单元、吸附单元、冷却单元、控制单元、安全装置单元、再生装置；该方法对废气净化彻底，吸附设备简单，处理效率高，但处理设备庞大，对吸附剂的要求较高。等离子法是通过高压放电形式，产生大量高能电子，从而破坏VOC中的化学键，最终生成0)2和H2O ;主要装置为等离子体反应器；设备装置简单，但能耗高，降解率低，且产生大量中间态污染物。光分解法是在一定波长的光照射或者利用某些催化剂的光催化特性，使有机物被分解；由于材料的限制，高能光子大多被灯管材料吸收，穿透玻璃的高能光子有限，故能效利用率低，去除效率一般，且产生大量中间态污染物。
发明内容
[0004] 本实用新型所要解决的技术问题是提供了一种含低浓度VOC废气的净化装置，解决了现有的含低浓度VOC废气净化装置中净化效果不彻底、成本高、中间态污染物多的技术难题。
[0005] 为解决上述问题，本实用新型的技术方案是:
[0006] 一种含低浓度VOC废气的净化装置，包括文丘里气固混合器、高效脉冲袋式除尘器、氧化塔、脱附装置、活性炭粉储罐、小型蓄热氧化炉、热交换器、涤气器、风机，所述的文丘里气固混合器排风口连接至高效脉冲袋式除尘器进风口，高效脉冲袋式除尘器顶部排风口连接至氧化塔进风口，氧化塔出口连接至风机；高效脉冲袋式除尘器灰斗经由粉剂流速调节阀连接至脱附装置，脱附装置底部出口连接至活性炭粉储罐，活性炭粉储罐出口经由粉剂流速调节阀连接至文丘里气固混合器，脱附装置顶部出口经由热交换器连接至小型蓄热氧化炉，小型蓄热氧化炉排风口经由热交换器连接至涤气器。
[0007] 优选的，所述的氧化塔内设有旋转式结构反应器；
[0008] 优选的，所述的脱附装置内设有导热油加热盘管；
[0009] 优选的，所述的小型蓄热氧化炉内设有余热回收装置；
[0010] 作为另一种方案，作为优选，脱附后的高浓度VOC可以不采用小型蓄热氧化炉氧化去除，还可以采用焚烧炉或吸收塔去除、回收有害物质。
[0011] 一种含低浓度VOC废气的净化装置，其实现方案包括下述步骤:
[0012] (I)将活性炭粉和含低浓度VOC废气通入文丘里气固混合器中混合；
[0013] (2)将吸附有VOC的活性炭粉与被吸附了 VOC后的废气通入高效脉冲袋式除尘器进行分离捕集；
[0014] (3)将高效脉冲袋式除尘器分离的废气通入氧化塔净化处理，净化处理后的洁净气体通过风机外排；
[0015] (4)将步骤⑵捕集的吸附有VOC的活性炭粉经由粉剂流速调节阀输送至脱附装置进行脱附再生处理；
[0016] (5)将脱附装置脱附再生后的活性粉输送至活性炭粉储罐收集、储存；
[0017] (6)将活性炭粉储罐内的活性炭粉经由粉剂流速调节阀输送至文丘里气固混合器;
[0018] (7)将脱附装置脱附出的含高浓度VOC废气经由热交换器连接至小型蓄热氧化炉进行净化处理，净化后的气体经由热交换器后通过涤气器外排。
[0019] 优选的，上述步骤(2)是将步骤(I)混合后的吸附有VOC的活性炭粉与被吸附了VOC后的废气进行有效分离捕集，分离后的废气通过净化塔进行氧化处理，吸附有VOC的活性炭粉经捕集进入脱附装置进行脱附处理。
[0020] 优选的，上述步骤(4)是将步骤(2)经捕集的吸附有VOC的活性炭粉在脱附装置内脱附，加热后的活性炭粉中的VOC从活性炭微孔中脱附出来，可使VOC浓度富集10〜15倍，降低后续处理设备的体积，活性炭得到再生。
[0021] 本实用新型的有益效果:本实用新型的结构设计使得含低浓度VOC废气的净化效率提高；极大提高吸附材料的比表面积后使得吸附材料用量减少，降低成本；采用高效脉冲袋式除尘器使得系统阻力得以降低，降低系统运行的动力消耗，将吸附有VOC的活性炭粉与被吸附了 VOC后的废气进行分离，废气得到第一步净化，净化后的废气通过后续氧化塔进行氧化处理，使废气得到彻底的净化，解决了常规处理装置处理不彻底的难题；脱附装置将VOC在高温下从活性炭粉内部微孔中脱附，活性炭粉得到再生；脱附出来的高浓度VOC废气通过小型蓄热氧化炉充分热氧化处理后，将VOC彻底降解，无二次污染，产生的热量由热交换器回用，该法与直接采用热氧化法处理相比极大地降低了燃料成本；再生的活性炭粉回流至活性炭粉储槽收集、储存，达到循环利用活性炭粉的目的；本装置的处理流程简单，解决了现有技术处理效果不彻底、处理成本较高、中间态污染物多的技术问题。
附图说明
[0022] 图1是本实用新型结构示意图。
[0023] 图中:1-文丘里气固混合器，2-高效脉冲袋式除尘器，3-氧化塔，4-风机，5、8_粉剂流速调节阀，6-脱附装置，7-活性炭粉储罐，9-热交换器，10-小型蓄热氧化炉，11-涤气器。
具体实施方式
[0024] 下面结合附图对本实用新型作进一步描述。
[0025] 如图1所示，本实用新型包括文丘里气固混合器1，高效脉冲袋式除尘器2，氧化塔3，风机4，粉剂流速调节阀5、8，脱附装置6，活性炭粉储罐7，热交换器9，小型蓄热氧化炉10，涤气器11 ;文丘里气固混合器I连接至高效脉冲袋式除尘器2，高效脉冲袋式除尘器2顶部排风口连接至氧化塔3，氧化塔3出口连接至风机4，高效脉冲袋式除尘器2灰斗连接至脱附装置6，脱附装置6底部出口连接至活性炭粉储罐7，活性炭粉储罐7出口连接至文丘里气固混合器1，脱附装置6顶部出口通过热交换器9连接至小型蓄热氧化炉10，小型蓄热氧化炉10通过热交换器9连接至涤气器11。
[0026] 含低浓度VOC废气从文丘里气固混合器I入口处进入，含低浓度VOC废气与活性炭粉在文丘里气固混合器I中均匀混合，混合后的废气与活性炭吸附粉一起至高效脉冲袋式除尘器2中，在此期间，活性炭粉快速吸附废气中的V0C，吸附有VOC的活性炭粉被高效脉冲袋式除尘器2的布袋捕集，分离出的含极少量VOC的废气通过高效脉冲袋式除尘器2排气口进入氧化塔3进行进一步净化处理，净化后的气体经由风机4外排。高效脉冲袋式除尘器2灰斗出来的吸附有VOC的活性炭粉经由粉剂流速调节阀5输送至脱附装置6脱附处理。脱附装置6脱附再生后的活性炭粉通过输送装置输送至活性炭粉储罐7。活性炭粉储罐7内活性炭粉经由粉剂流速调节阀8输送至文丘里气固混合器I。脱附装置6能够使VOC从活性炭表面脱附出来，脱附出来的高浓度VOC废气经过热交换器9后通过小型蓄热氧化炉10氧化分解，氧化分解后的气体经过热交换器9后通过涤气器11洗涤排放。
[0027] 本实用新型中，通过文丘里气固混合器I将含低浓度VOC废气与活性炭粉充分混合；通过高效脉冲袋式除尘器2将吸附有VOC的活性炭粉与被吸附了 VOC后的废气分离捕集；通过氧化塔3使强氧化剂和残余VOC充分混合、反应，达到去除残余VOC的目的。脱附装置6内设有导热油加热盘管，吸附后的活性炭粉与热盘管接触后升温，从而将活性炭粉中已吸附的VOC脱附出来，活性炭粉得到再生；再生的活性炭粉收集、储存至活性炭粉储罐7，达到循环利用活性炭粉的目的；小型蓄热氧化炉10内将脱附装置脱附出的含高浓度VOC的废气直接氧化成二氧化碳、水等，不产生二次污染，产生的热量由热交换器9回用，节省了资源。
[0028] 实施例2:
[0029]由于小型蓄热氧化炉10可以换成焚烧炉、吸收塔等装置中的一种或多种，其余均与实施例1相同，这里不再阐述。
[0030] 最后，应当指出，以上实施例仅是本实用新型较有代表性的例子。显然，本实用新型不限于上述实施例，还可以有许多变形。凡是依据本实用新型的技术实质对以上实施例所作的任何简单修改、等同变化与修饰，均应认为属于本实用新型的保护范围。
Claims (4)
1.一种含低浓度VOC废气的净化装置，其特征在于所述的VOC净化装置包括文丘里气固混合器、高效脉冲袋式除尘器、氧化塔、脱附装置、活性炭粉储槽、小型蓄热氧化炉、热交换器、涤气器、风机；所述的文丘里气固混合器出口处连接至高效脉冲袋式除尘器，高效脉冲袋式除尘器排风口连接至氧化塔进风口，氧化塔出口连接至风机，高效脉冲袋式除尘器灰斗连接至脱附装置，脱附装置底部出口连接至活性炭粉储罐，活性炭粉储罐出口连接至文丘里气固混合器，脱附装置顶部出口通过热交换器连接至小型蓄热氧化炉，小型蓄热氧化炉排风口通过热交换器连接至涤气器；所述的氧化塔内设有旋转式结构反应器，所述的脱附装置内设有导热油加热盘管，所述的小型蓄热氧化炉内设有余热回收装置；所述的小型蓄热氧化炉还可以是焚烧炉、吸收塔。
2.根据权利要求1所述的含低浓度VOC废气的净化装置，其特征在于，所述的净化装置内设有能够分离捕集吸附有VOC的活性炭粉与被吸附了 VOC后的废气的高效脉冲袋式除尘器。
3.根据权利要求1所述的含低浓度VOC废气的净化装置，其特征在于，所述的净化装置内设有可将活性炭粉不断再生的脱附装置。
4.根据权利要求1所述的含低浓度VOC废气的净化装置，其特征在于，所述的净化装置内设有收集、储存再生后活性炭粉的活性炭粉储鍾。
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| CN106139840A (zh) * | 2015-04-16 | 2016-11-23 | 杭州中兵环保股份有限公司 | 含低浓度voc废气的净化装置及方法 |
| CN106310847A (zh) * | 2016-09-14 | 2017-01-11 | 广东电网有限责任公司电力科学研究院 | 一种富氧燃烧锅炉烟气净化与资源化回收系统及工艺 |
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| CN106139840A (zh) * | 2015-04-16 | 2016-11-23 | 杭州中兵环保股份有限公司 | 含低浓度voc废气的净化装置及方法 |
| CN106310847A (zh) * | 2016-09-14 | 2017-01-11 | 广东电网有限责任公司电力科学研究院 | 一种富氧燃烧锅炉烟气净化与资源化回收系统及工艺 |
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