CN117105393A - Waste water treatment device based on photoelectric biological Fenton reaction - Google Patents
Waste water treatment device based on photoelectric biological Fenton reaction Download PDFInfo
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 34
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 27
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000002351 wastewater Substances 0.000 claims abstract description 24
- 229910052742 iron Inorganic materials 0.000 claims abstract description 18
- 238000012377 drug delivery Methods 0.000 claims abstract description 14
- 230000005611 electricity Effects 0.000 claims abstract description 11
- 239000003814 drug Substances 0.000 claims abstract description 8
- 244000005700 microbiome Species 0.000 claims abstract description 8
- 229940079593 drug Drugs 0.000 claims abstract description 6
- 230000001105 regulatory effect Effects 0.000 claims description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 239000002131 composite material Substances 0.000 claims description 8
- 239000011941 photocatalyst Substances 0.000 claims description 8
- 229910002804 graphite Inorganic materials 0.000 claims description 7
- 239000010439 graphite Substances 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000012528 membrane Substances 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- SZVJSHCCFOBDDC-UHFFFAOYSA-N ferrosoferric oxide Chemical compound O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 3
- 239000003292 glue Substances 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- 239000012258 stirred mixture Substances 0.000 claims description 3
- 239000004408 titanium dioxide Substances 0.000 claims description 3
- 238000013329 compounding Methods 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 7
- 239000010802 sludge Substances 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 238000004064 recycling Methods 0.000 abstract description 5
- 238000005276 aerator Methods 0.000 abstract description 4
- -1 iron ions Chemical class 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 abstract description 3
- 238000006555 catalytic reaction Methods 0.000 abstract description 3
- 238000011065 in-situ storage Methods 0.000 abstract description 3
- 230000029553 photosynthesis Effects 0.000 abstract description 3
- 238000010672 photosynthesis Methods 0.000 abstract description 3
- 150000003254 radicals Chemical class 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract description 2
- VSZGPKBBMSAYNT-RRFJBIMHSA-N oseltamivir Chemical compound CCOC(=O)C1=C[C@@H](OC(CC)CC)[C@H](NC(C)=O)[C@@H](N)C1 VSZGPKBBMSAYNT-RRFJBIMHSA-N 0.000 description 8
- 229960003752 oseltamivir Drugs 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001027 hydrothermal synthesis Methods 0.000 description 2
- 230000004792 oxidative damage Effects 0.000 description 2
- 238000007146 photocatalysis Methods 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000003443 antiviral agent Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 208000037797 influenza A Diseases 0.000 description 1
- 208000037798 influenza B Diseases 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 239000003642 reactive oxygen metabolite Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/005—Combined electrochemical biological processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Organic Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Molecular Biology (AREA)
- General Chemical & Material Sciences (AREA)
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- Health & Medical Sciences (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本发明提供了一种基于光电生物芬顿反应的废水处理器,通过产电微生物可以原位发电,减少了对外部电源的依赖,在提高转化效率的同时,满足多场景废水处理的需求,而阴极室的固定化微藻在光合作用下提供自由基的氧气,促进催化反应也替代了曝气器;通过控制单元和药品投放装置的设置可自动调节废水的pH,以及调节阴极和阳极阻值的大小,提高了废水处理效率。通过生物在电化学系统的应用,替代了外部能源以及仪器的使用,具有环境友好性,同时废水处理过程中产生Fe2+在反应中还原成Fe3+,而Fe3+在芬顿反应中充当催化剂以循环利用,减少了铁泥的生成;铁泥的减少和铁离子的循环使用既提高了芬顿反应的效率,又减少对新铁离子的需求和药品的消耗。
The present invention provides a wastewater processor based on the photoelectric bio-Fenton reaction, which can generate electricity in situ through electricity-producing microorganisms, reducing dependence on external power sources. While improving conversion efficiency, it can meet the needs of wastewater treatment in multiple scenarios. The immobilized microalgae in the cathode chamber provide free radical oxygen under photosynthesis, promote catalytic reactions and replace the aerator; the pH of the wastewater can be automatically adjusted through the settings of the control unit and drug delivery device, as well as the resistance of the cathode and anode. size, improving wastewater treatment efficiency. Through the application of biology in the electrochemical system, it replaces the use of external energy and instruments, and is environmentally friendly. At the same time, Fe 2+ produced during the wastewater treatment process is reduced to Fe 3+ in the reaction, and Fe 3+ is used in the Fenton reaction Acting as a catalyst for recycling, reducing the generation of iron sludge; the reduction of iron sludge and the recycling of iron ions not only improve the efficiency of the Fenton reaction, but also reduce the need for new iron ions and the consumption of medicines.
Description
技术领域Technical field
本发明涉及废水处理装置技术领域,具体而言,涉及一种基于光电生物芬顿反应的废水处理装置。The present invention relates to the technical field of wastewater treatment devices, and specifically to a wastewater treatment device based on photoelectric bio-Fenton reaction.
背景技术Background technique
奥司他韦作为一种最常用的抗病毒药物,在甲型和乙型流感的治疗中被广泛应用。由于含有奥司他韦药物的大规模使用,导致废水中奥司他韦的浓度大大增加,同时奥司他韦还可以通过水循环进入饮用水源,对人类健康构成潜在风险。Oseltamivir is the most commonly used antiviral drug and is widely used in the treatment of influenza A and B. Due to the large-scale use of drugs containing oseltamivir, the concentration of oseltamivir in wastewater has greatly increased. At the same time, oseltamivir can also enter drinking water sources through water circulation, posing potential risks to human health.
传统的有机废水处理技术多采用普通的气浮,吸附,过滤,臭氧氧化,氯化法,微电解等方法,而奥司他韦属于一类难降解的有机物,采用这些工艺普遍存在处理效率低下。而现有的芬顿反应器虽能提高处理效率,但其存在以下不足:Traditional organic wastewater treatment technologies mostly use ordinary air flotation, adsorption, filtration, ozone oxidation, chlorination, micro-electrolysis and other methods. Oseltamivir belongs to a type of organic matter that is difficult to degrade, and the treatment efficiency of these processes is generally low. . Although the existing Fenton reactor can improve treatment efficiency, it has the following shortcomings:
1.需要额外电源及设备使整个反应器进行作业,例如曝气器等;1. Additional power supply and equipment are required to operate the entire reactor, such as aerators, etc.;
2.反应过程中不断生成铁泥,大大降低了芬顿反应的效率;2. Iron sludge is continuously generated during the reaction, which greatly reduces the efficiency of the Fenton reaction;
3.无法自动调节废水中的pH值,以提高废水处理的效率。3. The pH value in wastewater cannot be automatically adjusted to improve the efficiency of wastewater treatment.
发明内容Contents of the invention
有鉴于此,本发明的目的在于提供一种基于光电生物芬顿反应的废水处理器。In view of this, the object of the present invention is to provide a wastewater treatment device based on photoelectric bio-Fenton reaction.
本发明采用了如下方案:The present invention adopts the following solutions:
本申请提供了一种基于光电生物芬顿反应的废水处理器,包括阳极室和阴极室,还包括有调节池、控制单元以及药品投放装置;This application provides a wastewater treatment device based on the photoelectric bio-Fenton reaction, which includes an anode chamber and a cathode chamber, as well as a regulating pool, a control unit and a drug delivery device;
所述控制单元用于调节所述阴极室和所述阳极室中阴极和阳极的电阻,以及控制所述药品投放装置向所述调节池以及所述阴极室投放药品;所述调节池被配置为:往所述阴极室单向输送废水;The control unit is used to adjust the resistance of the cathode and anode in the cathode chamber and the anode chamber, and to control the drug delivery device to release drugs into the adjustment pool and the cathode chamber; the adjustment pool is configured as : One-way transportation of waste water to the cathode chamber;
所述阳极室和所述阴极室之间由质子交换膜隔开;所述阳极室中采用碳刷作为阳极,且所述阳极室内放入有产电微生物;所述阴极室中采用石墨棒作为阴极,且所述石墨棒的表面涂覆有由磁性铁基复合光催化剂和导电胶搅拌均匀形成的混合物;所述阴极室投放有固定化微藻;所述阳极和所述阴极通过导线连接。The anode chamber and the cathode chamber are separated by a proton exchange membrane; a carbon brush is used as an anode in the anode chamber, and electricity-producing microorganisms are placed in the anode chamber; graphite rods are used in the cathode chamber as an anode. The cathode, and the surface of the graphite rod is coated with a uniformly stirred mixture of magnetic iron-based composite photocatalyst and conductive glue; immobilized microalgae is placed in the cathode chamber; the anode and the cathode are connected by wires.
进一步地,所述磁性铁基复合光催化剂由磁性四氧化三铁、氮掺杂二氧化钛和还原氧化石墨烯通过水热法复合制得。Further, the magnetic iron-based composite photocatalyst is composited by a hydrothermal method from magnetic ferroferric oxide, nitrogen-doped titanium dioxide and reduced graphene oxide.
进一步地,所述阳极室为密闭的腔室。Further, the anode chamber is a sealed chamber.
进一步地,所述药品投放装置存放有Na2S2O3、H2SO4和FeSO4。Further, the drug delivery device stores Na2S2O3, H2SO4 and FeSO4.
进一步地,所述调节池内还设置有与所述控制单元电连接的搅拌器和PH计。Further, a stirrer and a pH meter electrically connected to the control unit are also provided in the regulating tank.
进一步地,所述调节池内还设置有与所述述控制单元电连接的计量泵。Furthermore, a metering pump electrically connected to the control unit is also provided in the regulating tank.
进一步地,所述调节池与所述阴极室之间设置有与所述控制单元电连接的阀门开关,在所述阀门开关的下游设置有单向阀。Further, a valve switch electrically connected to the control unit is provided between the conditioning tank and the cathode chamber, and a one-way valve is provided downstream of the valve switch.
进一步地,所述调节池与所述连通道形成有高度差,所述阀门开关置于所述调节池的底部。Further, a height difference is formed between the regulating tank and the connecting channel, and the valve switch is placed at the bottom of the regulating tank.
通过采用上述技术方案,本发明可以取得以下技术效果:By adopting the above technical solutions, the present invention can achieve the following technical effects:
1、装置中通过产电微生物可以原位发电,减少了对外部电源的依赖,在提高转化效率的同时,满足多场景废水处理的需求。1. The device can generate electricity in situ through electricity-producing microorganisms, reducing dependence on external power sources. While improving conversion efficiency, it can meet the needs of wastewater treatment in multiple scenarios.
2、装置通过控制单元和药品投放装置的设置可自动调节废水的pH,以及调节阴极和阳极阻值的大小,提高了废水处理效率。2. The device can automatically adjust the pH of the wastewater through the settings of the control unit and the drug delivery device, as well as adjust the resistance of the cathode and anode, thereby improving the efficiency of wastewater treatment.
3、装置具有环境友好性,其废水处理过程中产生Fe2+在反应中还原成Fe3+,而Fe3+在芬顿反应中充当催化剂以循环利用,同时减少了铁泥的生成。3. The device is environmentally friendly. Fe2+ produced during the wastewater treatment process is reduced to Fe3+ in the reaction, and Fe3+ acts as a catalyst in the Fenton reaction for recycling, while reducing the generation of iron sludge.
附图说明Description of drawings
为了更清楚地说明本发明实施方式的技术方案,下面将对实施方式中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本发明的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly introduced below. It should be understood that the following drawings only show certain embodiments of the present invention and therefore do not It should be regarded as a limitation of the scope. For those of ordinary skill in the art, other relevant drawings can be obtained based on these drawings without exerting creative efforts.
图1是本发明实施例一种基于光电生物芬顿反应的废水处理器的结构示意图;Figure 1 is a schematic structural diagram of a wastewater treatment device based on photoelectric bio-Fenton reaction according to an embodiment of the present invention;
图2是本发明实施例一种基于光电生物芬顿反应的废水处理器剖面结构示意图。Figure 2 is a schematic cross-sectional structural diagram of a wastewater treatment device based on photoelectric bio-Fenton reaction according to an embodiment of the present invention.
图标:阴极室1,阳极室2、调节池3、控制单元4、药品投放装置5、阴极6、阳极7、质子交换膜8、PH计9、阀门开关10、搅拌器11。Icon: Cathode chamber 1, anode chamber 2, regulating tank 3, control unit 4, drug delivery device 5, cathode 6, anode 7, proton exchange membrane 8, pH meter 9, valve switch 10, stirrer 11.
具体实施方式Detailed ways
为使本发明实施方式的目的、技术方案和优点更加清楚,下面将结合本发明实施方式中的附图,对本发明实施方式中的技术方案进行清楚、完整地描述,显然,所描述的实施方式是本发明一部分实施方式,而不是全部的实施方式。基于本发明中的实施方式,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施方式,都属于本发明保护的范围。因此,以下对在附图中提供的本发明的实施方式的详细描述并非旨在限制要求保护的本发明的范围,而是仅仅表示本发明的选定实施方式。基于本发明中的实施方式,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施方式,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments These are some embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention. Accordingly, the following detailed description of embodiments of the invention provided in the appended drawings is not intended to limit the scope of the claimed invention, but rather to represent selected embodiments of the invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
实施例Example
结合图1和图2所示,本实施例提供了一种基于光电生物芬顿反应的废水处理器,包括阳极室2和阴极室1,还包括有调节池3、控制单元4以及药品投放装置5;As shown in FIGS. 1 and 2 , this embodiment provides a wastewater treatment device based on the photoelectric bio-Fenton reaction, which includes an anode chamber 2 and a cathode chamber 1 , a regulating pool 3 , a control unit 4 and a drug delivery device. 5;
所述控制单元4用于调节所述阴极室1和所述阳极室2中阴极6和阳极7的电阻,以及控制所述药品投放装置5向所述调节池3以及所述阴极室1投放药品;所述调节池3被配置为:往所述阴极室1单向输送废水;The control unit 4 is used to adjust the resistance of the cathode 6 and the anode 7 in the cathode chamber 1 and the anode chamber 2, and to control the medicine delivery device 5 to deliver medicine into the adjustment pool 3 and the cathode chamber 1 ; The regulating tank 3 is configured to: transport wastewater in one direction to the cathode chamber 1;
所述阳极室2和所述阴极室1之间由质子交换膜8隔开;所述阳极室2中采用碳刷作为阳极7,且所述阳极室2内放入有产电微生物;所述阴极室1中采用石墨棒作为阴极6,且所述石墨棒的表面涂覆有由磁性铁基复合光催化剂和导电胶搅拌均匀形成的混合物;所述阴极室1投放有固定化微藻;所述阳极7和所述阴极6通过导线连接。The anode chamber 2 and the cathode chamber 1 are separated by a proton exchange membrane 8; a carbon brush is used as the anode 7 in the anode chamber 2, and electricity-producing microorganisms are placed in the anode chamber 2; A graphite rod is used as the cathode 6 in the cathode chamber 1, and the surface of the graphite rod is coated with a uniformly stirred mixture of magnetic iron-based composite photocatalyst and conductive glue; immobilized microalgae is placed in the cathode chamber 1; so The anode 7 and the cathode 6 are connected through wires.
具体的,在本实施例中,所述磁性铁基复合光催化剂由磁性四氧化三铁、氮掺杂二氧化钛和还原氧化石墨烯通过水热法复合制得。所述阳极室2为密闭的腔室,确保产电微生物可以在厌氧环境下利用废水中的有机质生成电子和H+。所述磁性铁基复合光催化剂在自然光条件下催化O2生成活性氧,活性氧与阳极室2的H+反应生成H2O2同时为光催化提供氧气;而投放的固定化微藻则替代了曝气器的使用,既保护微藻免受活性氧的氧化损伤,又可以生成O2;所述药品投放装置5存放有Na2S2O3、H2SO4和FeSO4。在本实施例中,所述调节池3与所述阴极室1之间设置有与所述控制单元4电连接的阀门开关10,在所述阀门开关10的下游设置有单向阀(附图中未体现);所述调节池3与所述连通道形成有高度差,所述阀门开关10置于所述调节池3的底部,以使废水能通过重力势能通过所述连通道进入所述阴极室1;所述调节池3内还设置有与所述控制单元4电连接的搅拌器11和PH计9。当然,在其他实施例上,在所述调节池3与所述阴极室1之间还可以是在阀门开关10和单向阀的基础上增设计量泵,或是单独设置计量泵,用于为废水流向阴极室1提供动力,同时对废水进行计量,避免溢出阴极室1。Specifically, in this embodiment, the magnetic iron-based composite photocatalyst is made of magnetic ferroferric oxide, nitrogen-doped titanium dioxide and reduced graphene oxide through a hydrothermal method. The anode chamber 2 is a sealed chamber to ensure that electricity-producing microorganisms can utilize organic matter in wastewater to generate electrons and H + in an anaerobic environment. The magnetic iron-based composite photocatalyst catalyzes O 2 to generate active oxygen under natural light conditions, and the active oxygen reacts with H + in the anode chamber 2 to generate H 2 O 2 while providing oxygen for photocatalysis; while the immobilized microalgae replaced The use of an aerator not only protects microalgae from oxidative damage by active oxygen, but also generates O 2 ; the drug delivery device 5 stores Na 2 S 2 O 3 , H 2 SO 4 and FeSO 4 . In this embodiment, a valve switch 10 electrically connected to the control unit 4 is provided between the regulating tank 3 and the cathode chamber 1, and a one-way valve is provided downstream of the valve switch 10 (Fig. (not shown in ); there is a height difference between the regulating pool 3 and the connecting channel, and the valve switch 10 is placed at the bottom of the regulating pool 3 so that wastewater can enter the connecting channel through the gravity potential energy. The cathode chamber 1; the regulating tank 3 is also provided with a stirrer 11 and a pH meter 9 that are electrically connected to the control unit 4. Of course, in other embodiments, a metering pump can be added between the regulating tank 3 and the cathode chamber 1 on the basis of the valve switch 10 and the one-way valve, or a separate metering pump can be provided for The wastewater flows to the cathode chamber 1 to provide power, and at the same time, the wastewater is metered to avoid overflowing the cathode chamber 1.
以下详细说明该装置处理废水的过程:The following details the process of treating wastewater in this device:
奥司他韦废水通过调节池3的进水口进入调节池3,此时所述pH计9工作检测废水的pH值,并通过控制单元4控制所述药品投放装置5投放0.5mo l/L的H2SO4调节废水pH值至3左右,并投入0.5mo l/L的Na2SO4作为光生物电芬顿反应的电解质,以提高奥司他韦废水的导电性能;开启所述搅拌器11使以上药品充分均匀溶解在废水中,然后开启所述阀门开关10,让废水单向流入阴极室1进行芬顿反应;阴极室1中的所述磁性铁基复合光催化剂在自然光条件下催化O2生成活性氧;阳极7中的产电微生物在无氧的环境下利用废水中的有机质生成电子和产生H+,产生的电子有效传递给电极,H+通过质子交换膜8进入阴极室1;活性氧与H+反应生成H2O2同时为光催化提供氧气;而投放的固定化微藻,既保护微藻免受活性氧氧化损伤,又可以生成O2以促进催化反应;阴极室1中的Fe2+与H2O2反应生成·OH,生成的·OH的氧化还原电位较高,具有非常强的电子亲和力,可将奥司他韦废水降解为小分子的代谢产物或直接降解为二氧化碳和水;Fe2+作为消耗品所述药品投放装置5通过所述控制单元4可随时在所述阴极室1投放FeSO4以补充Fe2+。Oseltamivir wastewater enters the regulating pool 3 through the water inlet of the regulating pool 3. At this time, the pH meter 9 works to detect the pH value of the wastewater, and controls the drug delivery device 5 to release 0.5 mol/L through the control unit 4. H 2 SO 4 adjusts the pH value of the wastewater to about 3, and puts in 0.5 mol/L Na 2 SO 4 as the electrolyte for the photobioelectro-Fenton reaction to improve the electrical conductivity of the oseltamivir wastewater; turn on the stirrer 11 Let the above medicines be fully and evenly dissolved in the wastewater, and then open the valve switch 10 to allow the wastewater to flow into the cathode chamber 1 in one direction for Fenton reaction; the magnetic iron-based composite photocatalyst in the cathode chamber 1 catalyzes it under natural light conditions O 2 generates active oxygen; the electricity-producing microorganisms in the anode 7 use the organic matter in the wastewater to generate electrons and H+ in an oxygen-free environment. The generated electrons are effectively transferred to the electrode, and the H+ enters the cathode chamber 1 through the proton exchange membrane 8; active Oxygen reacts with H+ to generate H 2 O 2 while providing oxygen for photocatalysis; the immobilized microalgae not only protects the microalgae from oxidative damage by reactive oxygen species, but also generates O 2 to promote the catalytic reaction; in the cathode chamber 1 Fe 2+ reacts with H 2 O 2 to generate ·OH. The generated ·OH has a high redox potential and very strong electron affinity. It can degrade oseltamivir wastewater into small molecule metabolites or directly into carbon dioxide. and water; Fe 2+ as consumables. The drug delivery device 5 can deliver FeSO 4 into the cathode chamber 1 at any time through the control unit 4 to supplement Fe 2+ .
需要说明的是,阳极室2中的碳刷和阴极室1中的石墨棒通过导线连接,阳极7产生的电子通过导线传输至阴极6,确保阴极6化学反应的进行;而阴极6和阳极7之间可设置有可调电阻,通过控制单元4控制阻值以保证最佳芬顿反应的电流;同时该处理器的外壳可采用透明材质以保证微藻的光合作用。It should be noted that the carbon brush in the anode chamber 2 and the graphite rod in the cathode chamber 1 are connected through wires, and the electrons generated by the anode 7 are transmitted to the cathode 6 through the wires to ensure the chemical reaction of the cathode 6; while the cathode 6 and the anode 7 An adjustable resistor can be set between them, and the resistance value is controlled by the control unit 4 to ensure the best Fenton reaction current; at the same time, the shell of the processor can be made of transparent material to ensure the photosynthesis of microalgae.
本发明提供了一种基于光电生物芬顿反应的废水处理器,通过产电微生物可以原位发电,减少了对外部电源的依赖,在提高转化效率的同时,满足多场景废水处理的需求,而阴极室的固定化微藻在光合作用下提供自由基的氧气,促进催化反应,也替代了曝气器;通过控制单元4和药品投放装置5的设置可自动调节废水的pH,以及调节阴极6和阳极7阻值的大小,提高了废水处理效率。该废水处理器通过生物在电化学系统的应用,替代了外部能源以及仪器的使用,具有环境友好性,同时废水处理过程中产生Fe2+在反应中还原成Fe3+,而Fe3+在芬顿反应中充当催化剂以循环利用,减少了铁泥的生成;铁泥的减少和铁离子的循环使用既提高了芬顿反应的效率,又减少对新铁离子的需求和药品的消耗。The present invention provides a wastewater processor based on the photoelectric bio-Fenton reaction, which can generate electricity in situ through electricity-producing microorganisms, reducing dependence on external power sources. While improving conversion efficiency, it can meet the needs of wastewater treatment in multiple scenarios. The immobilized microalgae in the cathode chamber provide free radical oxygen under photosynthesis, promote catalytic reactions, and also replace the aerator; through the settings of the control unit 4 and the drug delivery device 5, the pH of the wastewater can be automatically adjusted, and the cathode 6 can be adjusted and the size of the resistance of the anode 7 improve the efficiency of wastewater treatment. This wastewater processor replaces the use of external energy and instruments through the application of biology in the electrochemical system, and is environmentally friendly. At the same time, Fe 2+ produced during the wastewater treatment process is reduced to Fe 3+ in the reaction, and Fe 3+ is Acting as a catalyst in the Fenton reaction for recycling, reducing the generation of iron sludge; the reduction of iron sludge and the recycling of iron ions not only improve the efficiency of the Fenton reaction, but also reduce the need for new iron ions and the consumption of medicines.
以上仅是本发明的优选实施方式,本发明的保护范围并不仅局限于上述实施例,凡属于本发明思路下的技术方案均属于本发明的保护范围。The above are only preferred embodiments of the present invention. The protection scope of the present invention is not limited to the above-mentioned embodiments. All technical solutions that fall under the idea of the present invention belong to the protection scope of the present invention.
在本发明的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的设备或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the present invention, it should be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", " The directions indicated by "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise" etc. or The positional relationship is based on the orientation or positional relationship shown in the drawings, which is only for the convenience of describing the present invention and simplifying the description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, Therefore, it should not be construed as a limitation of the present invention.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本发明的描述中,“多个”的含义是两个或两个以上,除非另有明确具体的限定。In addition, the terms “first” and “second” are used for descriptive purposes only and cannot be understood as indicating or implying relative importance or implicitly indicating the quantity of indicated technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include one or more of these features. In the description of the present invention, "plurality" means two or more than two, unless otherwise explicitly and specifically limited.
在本发明中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the present invention, unless otherwise clearly stated and limited, the terms "installation", "connection", "connection", "fixing" and other terms should be understood in a broad sense. For example, it can be a fixed connection or a detachable connection. , or integrated; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be an internal connection between two elements or an interaction between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.
在本发明中,除非另有明确的规定和限定,第一特征在第二特征之“上”或之“下”可以包括第一和第二特征直接接触,也可以包括第一和第二特征不是直接接触而是通过它们之间的另外的特征接触。而且,第一特征在第二特征“之上”、“上方”和“上面”包括第一特征在第二特征正上方和斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”包括第一特征在第二特征正下方和斜下方,或仅仅表示第一特征水平高度小于第二特征。In the present invention, unless otherwise expressly provided and limited, the term "above" or "below" a first feature of a second feature may include direct contact between the first and second features, or may also include the first and second features. Not in direct contact but through additional characteristic contact between them. Furthermore, the terms "above", "above" and "above" a first feature on a second feature include the first feature being directly above and diagonally above the second feature, or simply mean that the first feature is higher in level than the second feature. “Below”, “under” and “under” the first feature is the second feature includes the first feature being directly below and diagonally below the second feature, or simply means that the first feature is less horizontally than the second feature.
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