CN216614121U - A new type of electrocatalytic ammonia nitrogen wastewater treatment device - Google Patents
A new type of electrocatalytic ammonia nitrogen wastewater treatment device Download PDFInfo
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- CN216614121U CN216614121U CN202123278613.6U CN202123278613U CN216614121U CN 216614121 U CN216614121 U CN 216614121U CN 202123278613 U CN202123278613 U CN 202123278613U CN 216614121 U CN216614121 U CN 216614121U
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- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 8
- 239000003054 catalyst Substances 0.000 claims abstract description 17
- 238000006243 chemical reaction Methods 0.000 claims abstract description 8
- 230000000694 effects Effects 0.000 claims abstract description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000460 chlorine Substances 0.000 claims abstract description 6
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 6
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 claims description 6
- 239000002351 wastewater Substances 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000010941 cobalt Substances 0.000 claims description 3
- 229910017052 cobalt Inorganic materials 0.000 claims description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 claims description 2
- 239000005751 Copper oxide Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 229910000431 copper oxide Inorganic materials 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 230000009467 reduction Effects 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 abstract description 9
- 230000003647 oxidation Effects 0.000 abstract description 4
- 238000007254 oxidation reaction Methods 0.000 abstract description 4
- 239000006227 byproduct Substances 0.000 abstract description 3
- 238000005868 electrolysis reaction Methods 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000009471 action Effects 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 4
- 238000006555 catalytic reaction Methods 0.000 abstract 4
- 229910052757 nitrogen Inorganic materials 0.000 abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 238000010531 catalytic reduction reaction Methods 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 7
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(i) oxide Chemical compound [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 2
- -1 ammonia ions Chemical class 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- IYRDVAUFQZOLSB-UHFFFAOYSA-N copper iron Chemical compound [Fe].[Cu] IYRDVAUFQZOLSB-UHFFFAOYSA-N 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及水处理技术领域,具体是一种电催化氨氮废水处理系统。The utility model relates to the technical field of water treatment, in particular to an electrocatalytic ammonia nitrogen wastewater treatment system.
背景技术Background technique
对于高浓度污水氨氮污水来说,一般可采用空气吹脱法、蒸汽汽提法、 MAP沉淀法进行预处理,回收氨产品以补偿运行成本;对于中低浓度氨氮污水来说,传统技术采用生化法在硝化菌和反硝化菌作用下,进行硝化反硝化,但是在高盐废水中其作用会抑制,而且生化发去除氨氮反应需要添加各种药剂,提供培养条件培养生物菌,操作不便。因此电催化氧化法是一种很可靠的一种氨氮处理方法。For high-concentration ammonia nitrogen sewage, air stripping method, steam stripping method, and MAP precipitation method can generally be used for pretreatment, and ammonia products can be recovered to compensate for the operating cost; Under the action of nitrifying bacteria and denitrifying bacteria, nitrification and denitrification are carried out, but their effect will be inhibited in high-salt wastewater, and the biochemical removal of ammonia nitrogen requires the addition of various chemicals to provide culture conditions for culturing biological bacteria, which is inconvenient to operate. Therefore, electrocatalytic oxidation is a very reliable method for ammonia nitrogen treatment.
氨氮废水组份复杂,而废水中的氨氮大多以化合分子氨和氨离子和游离氨状态存在,氨氮氧化过程中发生反应为:氨氮电催化氧化后,会有部分以硝酸根形式存在,未能将副产物考虑在内,不能达标排放。The composition of ammonia nitrogen wastewater is complex, and most of the ammonia nitrogen in the wastewater exists in the state of compound molecular ammonia, ammonia ions and free ammonia. The reaction in the process of ammonia nitrogen oxidation is as follows: after the electrocatalytic oxidation of ammonia nitrogen, some of it exists in the form of nitrate, which fails to Taking into account the by-products, the emission standard cannot be met.
发明内容SUMMARY OF THE INVENTION
本实用新型的目的在于提供一种新型电催化氨氮废水处理装置。以解决上述背景技术中提出的问题。The purpose of this utility model is to provide a novel electrocatalytic ammonia nitrogen wastewater treatment device. In order to solve the problems raised in the above background art.
为实现上述目的,本实用新型提供如下技术方案:To achieve the above object, the utility model provides the following technical solutions:
一种新型电催化氨氮废水处理装置,其特征在于:包括所述阳极有电催化析氯活性的催化剂,阴极有电催化还原反硝化类催化剂。A novel electrocatalytic ammonia nitrogen wastewater treatment device is characterized in that: the anode has a catalyst with electrocatalytic chlorine evolution activity, and the cathode has an electrocatalytic reduction and denitrification catalyst.
作为本实用新型进一步的方案:所述阳极具有析氯活性高的催化剂,阳极催化剂是DSA电极、四氧化三钴电极、二氧化钌电极中的任意一种。As a further scheme of the present utility model: the anode has a catalyst with high chlorine evolution activity, and the anode catalyst is any one of a DSA electrode, a cobalt tetroxide electrode, and a ruthenium dioxide electrode.
作为本实用新型进一步的方案:所述阴极催化剂具有反硝化作用的催化剂,催化剂是铜电极,氧化铜电极、铁电极、氧化铁电极、碳电极中的任意一种。As a further scheme of the present utility model: the cathode catalyst has a catalyst for denitrification, and the catalyst is a copper electrode, any one of a copper oxide electrode, an iron electrode, an iron oxide electrode, and a carbon electrode.
与现有技术相比,本实用新型的有益效果是:Compared with the prior art, the beneficial effects of the present utility model are:
1.通过调节PH调节废水溶液至6-9,添加氯化钠,经过搅拌器搅拌,保证氯离子浓度为400以上,氯离子含量越多,能耗越低,电极反应两极板间的电压为 1.3v-10v。使用稳定性,活性高的析氯阳极材料,便于阳极析氯反应,能够促使氨氮转化更为彻底,使得整个阳极具有良好的稳定性与催化活性。1. Adjust the wastewater solution to 6-9 by adjusting the pH, add sodium chloride, and stir with a stirrer to ensure that the chloride ion concentration is above 400. The more chloride ion content, the lower the energy consumption. The voltage between the two electrode plates of the electrode reaction is 1.3v-10v. The chlorine-evolution anode material with high stability and activity is convenient for the anode chlorine-evolution reaction, which can promote the conversion of ammonia nitrogen more thoroughly, so that the whole anode has good stability and catalytic activity.
2.通过阴极反硝化,催化剂使用廉价易得的铁铜材料,有效的避免硝酸根副产物的生成,造成随意排放污染环境,具有较好的环保作用,整个设备结构简单,占地面积小,操作方便,使用的效果相对于传统方式更好。2. Through cathode denitrification, the catalyst uses cheap and readily available iron-copper materials, which effectively avoids the formation of nitrate by-products, causing random discharge to pollute the environment, and has a good environmental protection effect. The entire equipment has a simple structure and a small footprint. The operation is convenient, and the use effect is better than the traditional method.
附图说明Description of drawings
图1为氨氮处理整个装置的流程,包括预处理阶段和电催化氨氮反应阶段。Figure 1 shows the flow of the entire device for ammonia nitrogen treatment, including the pretreatment stage and the electrocatalytic ammonia nitrogen reaction stage.
图2为电催化阴阳电极载有催化剂示意图。Figure 2 is a schematic diagram of the electrocatalytic cathode and anode electrodes loaded with catalysts.
图3为电催化反应过程中氨氮和硝酸根含量随时间变化曲线。Figure 3 is the time-dependent curve of ammonia nitrogen and nitrate content during the electrocatalytic reaction.
图1中:1过滤器;2调节池;3泵;4电源及开关;5搅拌桨;6阳极; 7阴极;8阳极催化剂;9阴极催化剂。In Fig. 1: 1 filter; 2 regulating tank; 3 pump; 4 power supply and switch; 5 stirring paddle; 6 anode; 7 cathode; 8 anode catalyst; 9 cathode catalyst.
具体实施方式Detailed ways
下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,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例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, rather than all the implementations. example. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.
1.预处理阶段,待处理废液经过过滤,加入氢氧化钠和盐酸调节溶液的PH为6-9,最好接近于中性,调节氯离子浓度至400ppm-100000ppm,清洗阴极阳极上的附着物。1. In the pretreatment stage, the waste liquid to be treated is filtered, and sodium hydroxide and hydrochloric acid are added to adjust the pH of the solution to 6-9, preferably close to neutral, and the chloride ion concentration is adjusted to 400ppm-100000ppm. D.
2.电催化硝化反硝化阶段,2. Electrocatalytic nitrification and denitrification stage,
(1)实验采用阳极二氧化钌电极2cm*2cm,阴极使用铜-氧化铜电极2cm*2cm,打开搅拌器,设置电解电压2v,测试氨氮和硝酸根浓度随时间的变化,并与未加阴极反硝化电极的测试组做对比。(1) The experiment adopts the anode ruthenium dioxide electrode 2cm*2cm, the cathode uses the copper-copper oxide electrode 2cm*2cm, turns on the stirrer, sets the electrolysis voltage 2v, tests the change of ammonia nitrogen and nitrate concentration with time, and does not add the cathode. The test group of denitrification electrodes was compared.
(2)阳极使用四氧化三钴电极2cm*2cm,阴极使用铜-氧化铜电极2cm*2cm,打开搅拌器,设置电解电压2v,测试氨氮和硝酸根浓度随时间的变化。(2) Use a cobalt tetroxide electrode of 2cm*2cm for the anode and a copper-copper oxide electrode of 2cm*2cm for the cathode, turn on the stirrer, set the electrolysis voltage to 2v, and test the changes of ammonia nitrogen and nitrate concentration with time.
试验结果表明:反应500ml初始氨氮为100mg/L的废水,反应电流密度达到20mA左右,经过7小时左右时间,出水氨氮降为12mg/L,硝酸盐降低到 20mg/L以下,后期则在12mg/L左右。降解率达到88%,即出水水质达到排放标准。The test results show that the reaction current density of 500ml of wastewater with an initial ammonia nitrogen of 100mg/L reaches about 20mA. After about 7 hours, the ammonia nitrogen in the effluent is reduced to 12mg/L, the nitrate is reduced to below 20mg/L, and the latter is at 12mg/L. L or so. The degradation rate reaches 88%, that is, the effluent quality meets the discharge standard.
需要说明的是,在附图或说明书正文中,未绘制或描述的实现方法,均为所属技术领域中普通技术人员所知的形式,并未进行详细说明。此外,上述对各元件的定义并不限于实施例中提到的各种具体结构、形状或方法,不可进行简单的更改或替换。凡在本发明的精神和原则之内,所做的任何修改,均应该包含在本发明的保护范围之内。It should be noted that, in the drawings or the text of the description, the implementation methods that are not drawn or described are in the form known to those of ordinary skill in the technical field, and are not described in detail. In addition, the above definitions of each element are not limited to various specific structures, shapes or methods mentioned in the embodiments, and cannot be simply modified or replaced. Any modification made within the spirit and principle of the present invention should be included within the protection scope of the present invention.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115947422A (en) * | 2022-12-28 | 2023-04-11 | 南昌航空大学 | Method for efficiently mineralizing ammonia nitrogen by intensified chlorine evolution of metal electron-deficient configuration electric anode |
| CN116040756A (en) * | 2022-11-18 | 2023-05-02 | 同济大学 | Device and method for sequential electrical conversion treatment of nitrate coupled with fixed bed |
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2021
- 2021-12-24 CN CN202123278613.6U patent/CN216614121U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116040756A (en) * | 2022-11-18 | 2023-05-02 | 同济大学 | Device and method for sequential electrical conversion treatment of nitrate coupled with fixed bed |
| CN115947422A (en) * | 2022-12-28 | 2023-04-11 | 南昌航空大学 | Method for efficiently mineralizing ammonia nitrogen by intensified chlorine evolution of metal electron-deficient configuration electric anode |
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