CN115198288A - Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis - Google Patents
Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis Download PDFInfo
- Publication number
- CN115198288A CN115198288A CN202110316197.XA CN202110316197A CN115198288A CN 115198288 A CN115198288 A CN 115198288A CN 202110316197 A CN202110316197 A CN 202110316197A CN 115198288 A CN115198288 A CN 115198288A
- Authority
- CN
- China
- Prior art keywords
- water
- hydrogen peroxide
- air
- cathode chamber
- solenoid valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 246
- 239000001301 oxygen Substances 0.000 title claims abstract description 42
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 134
- 238000000746 purification Methods 0.000 claims abstract description 46
- 230000003197 catalytic effect Effects 0.000 claims abstract description 37
- 239000007784 solid electrolyte Substances 0.000 claims abstract description 37
- 238000007670 refining Methods 0.000 claims abstract description 36
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000003860 storage Methods 0.000 claims abstract description 33
- 239000012528 membrane Substances 0.000 claims abstract description 14
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 10
- 238000005341 cation exchange Methods 0.000 claims abstract description 8
- 239000003011 anion exchange membrane Substances 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 238000007254 oxidation reaction Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 6
- 229910002090 carbon oxide Inorganic materials 0.000 claims description 6
- 239000011347 resin Substances 0.000 claims description 6
- 229920005989 resin Polymers 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 238000006722 reduction reaction Methods 0.000 claims description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 239000008213 purified water Substances 0.000 claims description 4
- 239000004677 Nylon Substances 0.000 claims description 3
- 229910052797 bismuth Inorganic materials 0.000 claims description 3
- 239000002131 composite material Substances 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 239000000428 dust Substances 0.000 claims description 3
- 230000001678 irradiating effect Effects 0.000 claims description 3
- 229920001778 nylon Polymers 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 claims description 3
- 150000001450 anions Chemical class 0.000 claims description 2
- 239000003963 antioxidant agent Substances 0.000 claims description 2
- 230000003078 antioxidant effect Effects 0.000 claims description 2
- 239000007772 electrode material Substances 0.000 claims description 2
- 150000002978 peroxides Chemical class 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 6
- 238000000354 decomposition reaction Methods 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 12
- 239000000243 solution Substances 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005286 illumination Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 230000001699 photocatalysis Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000012429 reaction media Substances 0.000 description 2
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 description 1
- 150000004056 anthraquinones Chemical class 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010411 electrocatalyst Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 238000004076 pulp bleaching Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/28—Per-compounds
- C25B1/30—Peroxides
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Automation & Control Theory (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
本发明公开了一种水氧光电催化生产过氧化氢的一体化装置及制备方法,包括:水氧净化系统,具有进水管路和进气管路,配置为用于输送水和空气并对其净化;光电催化系统用于对水氧净化系统输送来的水和空气光电催化产生过氧化氢;存储精化系统对生产的过氧化氢检测、纯化,得到高纯过氧化氢;光电催化系统包括依次并列设置的阴极室、阴离子交换膜、固态电解质、阳离子交换膜与阳极室,阴极室上设置有进水口、进气口和出风口。该一体化装置能将水与空气高效转化为不同纯度与浓度的过氧化氢溶液,从而将光能与电能储存为过氧化氢的化学能,将过氧化氢的生产与提纯一体化集成,满足了高纯度过氧化氢溶液的随产随用,避免过氧化氢的分解与安全问题。
The invention discloses an integrated device and a preparation method for producing hydrogen peroxide by photoelectric catalysis of water and oxygen, comprising: a water-oxygen purification system, which has a water inlet pipeline and an air inlet pipeline, and is configured to transport and purify water and air. ; The photoelectric catalytic system is used to photoelectrically catalyze the water and air delivered by the water oxygen purification system to generate hydrogen peroxide; the storage refining system detects and purifies the produced hydrogen peroxide to obtain high-purity hydrogen peroxide; the photoelectric catalytic system includes the following steps: A cathode compartment, an anion exchange membrane, a solid electrolyte, a cation exchange membrane and an anode compartment are arranged in parallel, and the cathode compartment is provided with a water inlet, an air inlet and an air outlet. The integrated device can efficiently convert water and air into hydrogen peroxide solutions of different purities and concentrations, thereby storing light energy and electrical energy as the chemical energy of hydrogen peroxide, and integrating the production and purification of hydrogen peroxide to meet the The high-purity hydrogen peroxide solution can be used as it is produced to avoid the decomposition and safety problems of hydrogen peroxide.
Description
技术领域technical field
本发明属于合成过氧化氢技术领域,具体而言,涉及一种水氧光电催化生产高纯度过氧化氢的一体化装置及方法。The invention belongs to the technical field of synthesizing hydrogen peroxide, and in particular relates to an integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectric catalysis.
背景技术Background technique
过氧化氢是一种绿色化学品,广泛应用于消毒、水净化、工业纸浆漂白、化学合成和电子工业等领域。近年来,国际过氧化氢年需求量逐年增加,特别是东南亚、韩国、日本等地,过氧化氢供不应求,因而展现出巨大的市场潜力。过氧化氢的主要生产方式为蒽醌法,该方法虽然技术成熟,但能耗较大,且产生有机污染,因此严重制约了过氧化氢的发展。利用氢气和氧气直接合成过氧化氢是一种绿色节能的生产高纯过氧化氢的替代方案,但此过程中氢气和氧气的混合会带来安全问题,从而阻碍了该方法的实际应用。因此,研究的关注点逐渐转移到更安全、更高效的过氧化氢合成方法上。Hydrogen peroxide is a green chemical widely used in disinfection, water purification, industrial pulp bleaching, chemical synthesis and electronics industry. In recent years, the international annual demand for hydrogen peroxide has increased year by year, especially in Southeast Asia, South Korea, Japan and other places, the supply of hydrogen peroxide is in short supply, thus showing a huge market potential. The main production method of hydrogen peroxide is the anthraquinone method. Although this method is mature in technology, it consumes a lot of energy and produces organic pollution, which seriously restricts the development of hydrogen peroxide. The direct synthesis of hydrogen peroxide from hydrogen and oxygen is a green and energy-saving alternative to the production of high-purity hydrogen peroxide, but the mixing of hydrogen and oxygen in this process brings safety problems, which hinders the practical application of this method. Therefore, the research focus has gradually shifted to safer and more efficient hydrogen peroxide synthesis methods.
基于两电子转移的电化学氧化还原反应,即通过电催化同时将氧气和水转化为过氧化氢,是一种新兴的过氧化氢合成方式。与前两种生产工艺相比,该方法的优点在于:1)使用绿色天然资源,不消耗化石燃料;2)环境清洁,无有机废物;3)反应条件温和,无爆炸危险;4)理论上具有最高的能量转换效率。近年来,虽然研究人员在过氧化氢电催化剂的开发上取得了一定成就,但是基于水氧光电催化的过氧化氢规模化、现场化(on-site)生产仍具有局限性。Two-electron transfer-based electrochemical redox reactions, i.e. the simultaneous conversion of oxygen and water to hydrogen peroxide via electrocatalysis, is an emerging method for hydrogen peroxide synthesis. Compared with the first two production processes, the advantages of this method are: 1) using green natural resources, without consuming fossil fuels; 2) clean environment, no organic waste; 3) mild reaction conditions, no danger of explosion; 4) theoretically Has the highest energy conversion efficiency. In recent years, although researchers have made certain achievements in the development of hydrogen peroxide electrocatalysts, the large-scale and on-site production of hydrogen peroxide based on water-oxygen photocatalysis still has limitations.
发明内容SUMMARY OF THE INVENTION
本发明旨在提供一种水氧光电催化生产高纯度过氧化氢的一体化装置,能够将水与空气高效转化为不同纯度与浓度的过氧化氢溶液,从而将光能与电能储存为过氧化氢的化学能,实现过氧化氢溶液的随产随用。The invention aims to provide an integrated device for producing high-purity hydrogen peroxide by photoelectric catalysis of water and oxygen, which can efficiently convert water and air into hydrogen peroxide solutions of different purities and concentrations, so as to store light energy and electrical energy as peroxide The chemical energy of hydrogen enables the production and use of hydrogen peroxide solution.
为了实现上述目的,根据本发明的一个方面,提供了一种水氧光电催化生产高纯度过氧化氢的一体化装置,包括:水氧净化系统,具有进水管路和进气管路,分别配置为用于输送水和空气并对水和空气进行净化;光电催化系统,配置为用于对所述水氧净化系统输送来的水和空气光电催化产生过氧化氢;以及存储精化系统,对光电催化系统生产的过氧化氢进行检测、纯化,得到高纯过氧化氢;其中,光电催化系统包括依次并列设置的阴极室、固态电解质与阳极室,阴极室与所述固态电解质之间设置有阴离子交换膜,固态电解质与阳极室之间设置有阳离子交换膜;所述阴极室上设置有与水氧净化系统的进水管路连通的进水口、与进风管路连通的进气口和出风口。In order to achieve the above purpose, according to one aspect of the present invention, an integrated device for producing high-purity hydrogen peroxide by water-oxygen photoelectric catalysis is provided, comprising: a water-oxygen purification system, which has a water inlet pipeline and an air inlet pipeline, which are respectively configured as For transporting water and air and purifying water and air; a photoelectric catalytic system, configured to photoelectrically catalyze the water and air transported by the water and oxygen purification system to generate hydrogen peroxide; and a storage refining system for photoelectric The hydrogen peroxide produced by the catalytic system is detected and purified to obtain high-purity hydrogen peroxide; wherein, the photoelectric catalytic system includes a cathode chamber, a solid electrolyte and an anode chamber arranged in parallel in sequence, and an anion is arranged between the cathode chamber and the solid electrolyte. exchange membrane, a cation exchange membrane is arranged between the solid electrolyte and the anode chamber; the cathode chamber is provided with a water inlet connected with the water inlet pipeline of the water-oxygen purification system, an air inlet and an air outlet connected with the air inlet pipeline .
根据本发明,所述阳极室的一侧设置有辐照装置,配置为用于发射可见光光源以对阳极室辐照。According to the present invention, one side of the anode chamber is provided with an irradiation device configured to emit a visible light source to irradiate the anode chamber.
根据本发明,所述进水管路上依次设置有进水口、水流电磁阀、水压机、纯化柱、水流流速阀与进水通路电磁阀;所述进水通路电磁阀具有三个出口,分别与阴极室、固态电解质和阳极室连通。According to the present invention, the water inlet pipeline is provided with a water inlet, a water flow solenoid valve, a hydraulic press, a purification column, a water flow velocity valve and a water inlet passage solenoid valve in sequence; the water inlet passage solenoid valve has three outlets, which are respectively connected to the cathode chamber. , the solid electrolyte is communicated with the anode compartment.
根据本发明,所述进气管路上依次设置有进风口、空气泵、滤网和气体流速阀,所述气体流速阀与阴极室连通。According to the present invention, an air inlet, an air pump, a filter screen and a gas flow rate valve are sequentially arranged on the air inlet pipeline, and the gas flow rate valve communicates with the cathode chamber.
根据本发明,所述阴极室具有出口,所述出口依次连接止回阀和出风口。优选地,所述阴极室上配备有压力表。According to the present invention, the cathode chamber has an outlet, and the outlet is sequentially connected to the check valve and the air outlet. Preferably, the cathode chamber is equipped with a pressure gauge.
优选地,所述固态电解质的一端连接进水通路电磁阀,另一端连接检测器。Preferably, one end of the solid electrolyte is connected to the solenoid valve of the water inlet passage, and the other end is connected to the detector.
优选地,所述阳极室的一端连通进水通路电磁阀,另一端连接检测器。Preferably, one end of the anode chamber is connected to the electromagnetic valve of the water inlet passage, and the other end is connected to the detector.
根据本发明,所述存储精化系统还包括与光电催化系统连通且配置为用于对生产的过氧化氢质量检测的检测器。According to the present invention, the storage refinement system further includes a detector in communication with the photoelectric catalytic system and configured for quality detection of the produced hydrogen peroxide.
优选地,所述存储精化系统还包括与检测器依次连通的过氧化氢储罐、加压泵和气流电磁阀,所述过氧化氢储罐中的过氧化氢由加压泵经气流电磁阀的一端流出,得到高纯过氧化氢。Preferably, the storage refining system further comprises a hydrogen peroxide storage tank, a pressurizing pump and an air flow solenoid valve sequentially communicated with the detector, and the hydrogen peroxide in the hydrogen peroxide storage tank is passed through the air flow electromagnetic valve by the pressurizing pump One end of the valve flows out to obtain high-purity hydrogen peroxide.
优选地,所述存储精化系统还包括设置在气流电磁阀末端的精化柱,配置为用于对高纯过氧化氢进行精化,得到超高纯过氧化氢。Preferably, the storage refining system further includes a refining column arranged at the end of the gas flow solenoid valve, configured to refine the high-purity hydrogen peroxide to obtain ultra-high-purity hydrogen peroxide.
根据本发明,所述纯化柱为三段式纯化柱,包括依次设置的活性炭纯化柱、吸附树脂纯化柱与紫外氧化灯。优选地,所述滤网包括依次设置的除尘袋与干燥网两段式过滤结构。According to the present invention, the purification column is a three-stage purification column, including an activated carbon purification column, an adsorption resin purification column and an ultraviolet oxidation lamp which are arranged in sequence. Preferably, the filter screen includes a two-stage filter structure of a dust bag and a drying screen arranged in sequence.
根据本发明,所述检测器由可编程程序控制器、搭载DSP芯片的CPU模块以及数显屏构成,以实时检测过氧化氢溶液浓度和储量、机器内部工作状态、历史数据查询、耗材更换提示和故障报警。优选地,所述精化柱为两段式精化柱,包括具有抗氧化功能的吸附树脂精化柱与尼龙超滤膜精化柱。According to the present invention, the detector is composed of a programmable program controller, a CPU module equipped with a DSP chip, and a digital display screen to detect the concentration and storage of hydrogen peroxide solution, the internal working state of the machine, historical data query, and consumables replacement prompts in real time. and fault alarm. Preferably, the refining column is a two-stage refining column, including an adsorption resin refining column with anti-oxidation function and a nylon ultrafiltration membrane refining column.
根据本发明的另一方面,还提供了一种水氧光电催化生产高纯度过氧化氢的一体化方法,包括以下步骤:S1、打开水氧净化系统的进水管路和进气管路,使得水经水流电磁阀、通过水压机增压进入纯化柱并预纯化,预纯化后的水流在水流流速阀控制下经进水通路电磁阀进入光电催化系统;进气管路上的空气经空气泵增压,通过滤网过滤得到纯化空气,经流速阀调节,进入光电催化系统的阴极室;S2、调节阴极室内的气体流入与流出比,使其工作压力为0~1Mpa,纯化空气在阴极室发生氧还原反应,生成纯净过氧化氢,过氧化氢以HO2-的形式经位于阴极室与固态电解质之间的阴离子交换膜扩散进入固态电解质,多余空气由阴极室的另一端经止回阀、出风口流出设备;S3、预纯化后的水在阳极室发生水氧化反应,生成纯净过氧化氢和H+,过氧化氢被洗出阳极室,而H+沿阳极室与固态电解质之间的阳离子交换膜扩散进入固态电解质;S4、从阴极室扩散来的HO2-与从阳极室扩散来的H+结合生成H2O2,之后被水洗出光电催化系统;S5、所述光电催化系统生成的过氧化氢经检测器检测产品质量后,流入储罐备用;所述储罐中的过氧化氢经加压泵流入气流电磁阀,在气流电磁阀的一端流出设备,得到高纯过氧化氢;过氧化氢经气流电磁阀的另一端进入精化柱精化,得到超高纯过氧化氢。According to another aspect of the present invention, an integrated method for producing high-purity hydrogen peroxide by photoelectric catalysis of water and oxygen is also provided, comprising the following steps: S1. Open the water inlet pipeline and the air inlet pipeline of the water and oxygen purification system, so that the water After passing through the water flow solenoid valve, it is pressurized by the hydraulic press to enter the purification column and pre-purified. The pre-purified water flow enters the photoelectric catalytic system through the water inlet passage solenoid valve under the control of the water flow velocity valve; the air on the intake pipe is pressurized by the air pump, and the The purified air is filtered by the filter screen, which is adjusted by the flow rate valve and enters the cathode chamber of the photoelectric catalytic system; S2. Adjust the gas inflow and outflow ratio in the cathode chamber to make the working pressure 0-1Mpa, and the purified air will undergo oxygen reduction reaction in the cathode chamber. , generate pure hydrogen peroxide, hydrogen peroxide diffuses into the solid electrolyte in the form of HO 2- through the anion exchange membrane between the cathode chamber and the solid electrolyte, and the excess air flows out from the other end of the cathode chamber through the check valve and the air outlet Equipment; S3, the water after pre-purification undergoes water oxidation reaction in the anode chamber to generate pure hydrogen peroxide and H + , the hydrogen peroxide is washed out of the anode chamber, and H + along the cation exchange membrane between the anode chamber and the solid electrolyte Diffusion into the solid electrolyte; S4, HO 2- diffused from the cathode chamber combines with H + diffused from the anode chamber to form H 2 O 2 , which is then washed out of the photoelectric catalytic system; After the product quality is detected by the detector, the hydrogen peroxide flows into the storage tank for use; the hydrogen peroxide in the storage tank flows into the airflow solenoid valve through the pressurized pump, and flows out of the equipment at one end of the airflow solenoid valve to obtain high-purity hydrogen peroxide; The hydrogen oxide enters the refining column through the other end of the gas flow solenoid valve and is refined to obtain ultra-high-purity hydrogen peroxide.
根据本发明,所述光电催化系统的阴极室的主要材料为多孔氧化碳纸,工作面积100cm2,工作电流密度0.2A/cm2,阴极室的工作压力为0~1Mpa。优选地,所述阳极室电极材料为多孔氧化碳纸-钒酸铋复合材料,有效工作面积为100cm2,工作电流密度0.2A/cm2。优选地,进气管路上的空气流经气体流速阀调节后以100mL/min的流速进入光电催化系统。According to the present invention, the main material of the cathode chamber of the photoelectric catalytic system is porous carbon oxide paper, the working area is 100cm 2 , the working current density is 0.2A/cm 2 , and the working pressure of the cathode chamber is 0-1Mpa. Preferably, the anode chamber electrode material is a porous carbon oxide paper-bismuth vanadate composite material, the effective working area is 100 cm 2 , and the working current density is 0.2 A/cm 2 . Preferably, the air flow on the intake pipeline enters the photoelectric catalytic system at a flow rate of 100 mL/min after being adjusted by the gas flow rate valve.
优选地,所述固态电解质的材料为苯乙烯-二乙烯苯共聚物,厚度为0.5cm。优选地,步骤S3中还包括对阳极室进行辐照的过程,辐照的光源为可见光光源,功率为0~200W。优选地,水氧净化系统的供水流速为10~1000mL/h,空气泵的压力为20kPa,供气流速为100mL/分钟。Preferably, the material of the solid electrolyte is styrene-divinylbenzene copolymer, and the thickness is 0.5 cm. Preferably, step S3 also includes a process of irradiating the anode chamber, and the light source for irradiation is a visible light source with a power of 0-200W. Preferably, the water supply flow rate of the water and oxygen purification system is 10-1000mL/h, the pressure of the air pump is 20kPa, and the air supply flow rate is 100mL/min.
与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:
(1)本发明的一体化装置能够将水与空气高效转化为不同纯度与浓度的过氧化氢溶液,从而将光能与电能储存为过氧化氢的化学能,将过氧化氢的生产与提纯一体化集成,提供了一种中小规模生产高纯度过氧化氢溶液的解决方案,满足了超高纯度过氧化氢溶液的随产随用,避免过氧化氢在储存、运输途中出现的分解与安全问题。(1) The integrated device of the present invention can efficiently convert water and air into hydrogen peroxide solutions of different purities and concentrations, thereby storing light energy and electrical energy as the chemical energy of hydrogen peroxide, and purifying the production and purification of hydrogen peroxide Integrated integration provides a solution for small and medium-scale production of high-purity hydrogen peroxide solution, which satisfies the production and use of ultra-high-purity hydrogen peroxide solution, and avoids the decomposition and safety of hydrogen peroxide during storage and transportation. question.
(2)本发明使用绿色天然资源,对环境友好,且反应条件温和,无爆炸危险;在阴阳两极共催化合成高品质过氧化氢,理论上具有最高的能量转换效率。(2) The present invention uses green natural resources, is environmentally friendly, and has mild reaction conditions and no danger of explosion; co-catalyzed synthesis of high-quality hydrogen peroxide at the yin and yang poles, theoretically has the highest energy conversion efficiency.
(3)阴极室具备高压反应功能,氧气利用率高,电流密度大,产H2O2效率高;阳极室辅助以光照,将光能直接转化为高附加值化学品,节约电资源。(3) The cathode chamber has high-voltage reaction function, high oxygen utilization rate, high current density, and high H 2 O 2 production efficiency; the anode chamber is assisted by illumination, which directly converts light energy into high value-added chemicals and saves electricity resources.
附图说明Description of drawings
图1为本发明一种水氧光电催化生产高纯度过氧化氢的一体化装置的结构示意图。1 is a schematic structural diagram of an integrated device for producing high-purity hydrogen peroxide by water-oxygen photoelectric catalysis of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,下面结合本附图及实施例,对本发明做进一步的详细说明。需要强调,此处描述的具体实施例仅用于更好的阐述本发明,为本发明部分实施例,而非全部实施例,所以并不用作限定本发明。此外,下面描述的本发明实施例中涉及的技术特征,只要彼此间未构成冲突,即可以相互组合。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It should be emphasized that the specific embodiments described herein are only used to better illustrate the present invention, and are some rather than all embodiments of the present invention, so they are not intended to limit the present invention. In addition, the technical features involved in the embodiments of the present invention described below can be combined with each other as long as they do not conflict with each other.
如图1所示,本发明提供了一种水氧光电催化生产过氧化氢的一体化装置,包括水氧净化系统、光电催化系统和存储精化系统,其中水氧净化系统具有进水管路和进风管路,分别配置为用于输送水和氧气并对水和氧气进行净化。光电催化系统配置为用于对水氧净化系统输送来的水和氧气光电催化产生过氧化氢。存储精化系统对光电催化系统产生的过氧化氢进行检测、纯化,从而得到高纯过氧化氢。该一体化装置能够将水与空气高效转化为不同纯度与浓度的过氧化氢溶液,从而将光能与电能储存为过氧化氢的化学能,实现过氧化氢溶液的随产随用,为医疗、电子、食品等领域带来便利,同时避免过氧化氢在储存、运输过程中出现的分解与安全问题。As shown in FIG. 1 , the present invention provides an integrated device for the production of hydrogen peroxide by photoelectric catalysis of water and oxygen, including a water and oxygen purification system, a photoelectric catalytic system and a storage refining system, wherein the water and oxygen purification system has a water inlet pipeline and The air inlet pipes are respectively configured to transport and purify water and oxygen. The photoelectric catalytic system is configured to photoelectrically catalyze the water and oxygen delivered from the water oxygen purification system to generate hydrogen peroxide. The storage refining system detects and purifies the hydrogen peroxide produced by the photoelectric catalytic system to obtain high-purity hydrogen peroxide. The integrated device can efficiently convert water and air into hydrogen peroxide solutions of different purities and concentrations, so as to store light energy and electrical energy as the chemical energy of hydrogen peroxide, and realize the use of hydrogen peroxide solutions as they are produced and used for medical treatment. , electronics, food and other fields bring convenience, and at the same time avoid the decomposition and safety problems of hydrogen peroxide during storage and transportation.
如图1所示,水氧净化系统包括进水管路和进气管路,进水管路上依次设置有进水口、水流电磁阀1、水压机2、纯化柱3、水流流速阀4以及进水通路电磁阀5,其中进水通路电磁阀5具有三个出口,分别与阴极室9、固态电解质13和阳极室14连通。进入的水经水流电磁阀1到达水压机2,经其增压进入纯化柱3预纯化,预纯化水在水流流速阀4控制下以不同流速(10~1000mL/h)经进水通路电磁阀5进入光电催化系统。优选地,进水管路上的纯化柱3为三段式纯化柱,包括依次设置的活性炭纯化柱、吸附树脂纯化柱与紫外氧化灯。As shown in Figure 1, the water and oxygen purification system includes a water inlet pipeline and an air intake pipeline. The water inlet pipeline is sequentially provided with a water inlet, a water flow solenoid valve 1, a hydraulic press 2, a purification column 3, a water flow velocity valve 4 and a water inlet passage solenoid valve. 5, wherein the solenoid valve 5 of the water inlet passage has three outlets, which are respectively communicated with the cathode chamber 9, the solid electrolyte 13 and the anode chamber 14. The incoming water reaches the hydraulic press 2 through the water flow solenoid valve 1, and is pressurized into the purification column 3 for pre-purification. Enter the photocatalytic system. Preferably, the purification column 3 on the water inlet pipeline is a three-stage purification column, including an activated carbon purification column, an adsorption resin purification column and an ultraviolet oxidation lamp arranged in sequence.
如图1所示,进气管路上依次设置有进风口、空气泵6、滤网7和气体流速阀8,其中气体流速阀8与阴极室9连通。空气经进风口进入,再经空气泵6增压,通过滤网7过滤后得到纯化空气,经气体流速阀8调节,最终以100mL/min的流速进入光电催化系统。优选地,水氧净化系统的进风管路上的滤网7为两段式过滤,依次为除尘袋与干燥网。As shown in FIG. 1 , an air inlet, an air pump 6 , a filter screen 7 and a gas flow valve 8 are sequentially arranged on the air inlet pipeline, wherein the gas flow valve 8 communicates with the cathode chamber 9 . The air enters through the air inlet, is pressurized by the air pump 6, filtered through the filter screen 7 to obtain purified air, adjusted by the gas flow rate valve 8, and finally enters the photoelectric catalytic system at a flow rate of 100mL/min. Preferably, the filter screen 7 on the air inlet pipeline of the water-oxygen purification system is a two-stage filter, followed by a dust bag and a drying screen.
光电催化系统包括依次并列设置的阴极室9、固态电解质13与阳极室14。阴极室9与固态电解质13之间设置有阴离子交换膜16,固态电解质13与阳极室14之间设置有阳离子交换膜17。阴极室9上设置有与进水管路连通的进水口、与进气管路连通的进气口以及出口,所述出口依次连接止回阀11和出风口12。优选地,阴极室9上配备有压力表10。The photoelectric catalytic system includes a cathode chamber 9 , a solid electrolyte 13 and an anode chamber 14 which are arranged in parallel. An
其中,固态电解质13和阳极室14上均设置有进水口,分别与进水通路电磁阀5连通,另一端均与检测器18连通。优选地,所述阳极室14的一侧还设置有辐照装置,配置为用于发射可见光光源15以对阳极室14辐照。具体地,可见光光源15的功率为0~200W。Wherein, the solid electrolyte 13 and the anode chamber 14 are both provided with water inlets, which are respectively communicated with the solenoid valve 5 of the water inlet passage, and the other ends are both communicated with the detector 18 . Preferably, one side of the anode chamber 14 is further provided with an irradiation device configured to emit a visible light source 15 to irradiate the anode chamber 14 . Specifically, the power of the visible light source 15 is 0-200W.
如图1所示,存储精化系统还包括与固态电解质13连通且对生产的过氧化氢质量进行检测的检测器18。优选地,检测器18由可编程程序控制器、搭载DSP芯片的CPU模块以及数显屏构成,以实时检测过氧化氢溶液浓度和储量、机器内部工作状态、历史数据查询、耗材更换提示和故障报警。As shown in FIG. 1, the storage refinement system also includes a detector 18 in communication with the solid electrolyte 13 and which detects the quality of the hydrogen peroxide produced. Preferably, the detector 18 is composed of a programmable program controller, a CPU module equipped with a DSP chip, and a digital display screen to detect the concentration and storage of hydrogen peroxide solution, the internal working state of the machine, historical data query, consumables replacement prompts and faults in real time Call the police.
根据本发明,存储精化系统还包括与检测器18依次连通的过氧化氢储罐19、加压泵20和水流电磁阀21,催化系统生成的过氧化氢经检测器检18测产品质量后,流入过氧化氢储罐19备用。其中过氧化氢储罐19中的过氧化氢由加压泵20经水流电磁阀21的一端流出,得到高纯过氧化氢。在水流电磁阀21另一端还设置有精化柱22,配置为用于对高纯过氧化氢进行精化,过氧化氢经水流电磁阀21另一端进入精化柱22,得到超高纯过氧化氢。优选地,存储精化系统的精化柱22为两段式精化柱,包括具有抗氧化功能的吸附树脂精化柱与尼龙超滤膜精化柱。According to the present invention, the storage refining system further includes a hydrogen peroxide storage tank 19, a pressurizing pump 20 and a water flow solenoid valve 21 which are sequentially communicated with the detector 18. After the hydrogen peroxide generated by the catalytic system is checked by the detector 18 to detect the quality of the product , flow into the hydrogen peroxide storage tank 19 for standby. The hydrogen peroxide in the hydrogen peroxide storage tank 19 flows out from the pressure pump 20 through one end of the water flow solenoid valve 21 to obtain high-purity hydrogen peroxide. The other end of the water flow solenoid valve 21 is also provided with a refining column 22, which is configured for refining high-purity hydrogen peroxide. The hydrogen peroxide enters the refining column 22 through the other end of the water flow solenoid valve 21 to obtain ultra-high-purity hydrogen peroxide. hydrogen oxide. Preferably, the refining column 22 of the storage refining system is a two-stage refining column, including an adsorption resin refining column with antioxidant function and a nylon ultrafiltration membrane refining column.
根据本发明的另一方面,还提供了一种水氧光电催化生产过氧化氢的一体化方法,包括以下步骤:S1、打开水氧净化系统的进水管路和进气管路,使得水经水流电磁阀1、通过水压机2增压进入纯化柱3并预纯化,预纯化后的水在水流流速阀4控制下经过进水通路电磁阀5进入光电催化系统;进气管路上的空气经空气泵6增压,通过滤网7过滤得到纯化空气,经气体流速阀8调节,进入光电催化系统的阴极室9。According to another aspect of the present invention, an integrated method for producing hydrogen peroxide by photoelectric catalysis of water and oxygen is also provided, comprising the following steps: S1. Open the water inlet pipeline and the air inlet pipeline of the water oxygen purification system, so that the water flows through the water flow. Solenoid valve 1, pressurized by hydraulic press 2 into purification column 3 and pre-purified, the pre-purified water enters the photoelectric catalytic system through solenoid valve 5 of water inlet passage under the control of water flow velocity valve 4; the air on the intake pipe passes through air pump 6 Pressurized, filtered through the filter screen 7 to obtain purified air, adjusted by the gas flow rate valve 8, and entered into the cathode chamber 9 of the photoelectric catalytic system.
S2、调节阴极室9内的气体流入与流出比,使其工作压力为0~1Mpa,纯化空气在阴极室9发生氧还原反应,生成纯净过氧化氢,过氧化氢以HO2-的形式经位于阴极室9与固态电解质13之间的阴离子交换膜16扩散进入固态电解质13,多余空气由阴极室9的另一端经止回阀10、出风口11流出。S2, adjust the gas inflow and outflow ratio in the cathode chamber 9, make its working pressure be 0~1Mpa, the oxygen reduction reaction of the purified air takes place in the cathode chamber 9, generate pure hydrogen peroxide, and the hydrogen peroxide is passed through in the form of HO 2- The
S3、预纯化后的水在阳极室14发生水氧化反应,生成纯净过氧化氢和H+,过氧化氢被洗出阳极室14,而H+沿阳极室14与固态电解质13之间的阳离子交换膜17扩散进入固态电解质13。S3, the water after the pre-purification undergoes water oxidation reaction in the anode chamber 14 to generate pure hydrogen peroxide and H + , the hydrogen peroxide is washed out of the anode chamber 14 , and H + along the positive ions between the anode chamber 14 and the solid electrolyte 13 The
S4、从阴极室9扩散来的HO2-与从阳极室14扩散来的H+结合生成H2O2,之后被水洗出光电催化系统。S4. HO 2- diffused from the cathode chamber 9 combines with H + diffused from the anode chamber 14 to form H 2 O 2 , which is then washed out of the photoelectric catalytic system by water.
S5、经光电催化系统催化产生的过氧化氢,经检测器18检测产品质量后流入储罐19备用;所述储罐19中的过氧化氢经加压泵20流入水流电磁阀21,在水流电磁阀21的一端流出设备,得到高纯过氧化氢;过氧化氢经水流电磁阀21的另一端进入精化柱22精化,得到超高纯过氧化氢。S5. The hydrogen peroxide catalyzed by the photoelectric catalytic system flows into the storage tank 19 for standby after the product quality is detected by the detector 18; One end of the solenoid valve 21 flows out of the equipment to obtain high-purity hydrogen peroxide; the hydrogen peroxide enters the refining column 22 through the other end of the water flow solenoid valve 21 for refining to obtain ultra-high-purity hydrogen peroxide.
优选地,所述步骤S3中还包括对阳极室14进行辐照的过程,辐照的光源为可见光光源15,功率为0~200W。Preferably, the step S3 further includes a process of irradiating the anode chamber 14 , and the light source for irradiation is a visible light source 15 with a power of 0-200W.
根据本发明,光电催化系统的阴极室9的主要材料为多孔氧化碳纸,有效工作面积100cm2,工作电流密度0.2A/cm2,阴极室9的工作压力为0~1Mpa。纯化空气在阴极室9发生氧还原反应,生成纯净过氧化氢,过氧化氢以HO2-的形式经过阴离子交换膜16扩散进入固态电解质13,与来自阳极的H+离子结合生成H2O2,之后被水洗出光电催化系统。多余空气由阴极室9的另一端经止回阀11、出风口12流出设备。According to the present invention, the main material of the cathode chamber 9 of the photoelectric catalytic system is porous carbon oxide paper, the effective working area is 100cm 2 , the working current density is 0.2A/cm 2 , and the working pressure of the cathode chamber 9 is 0-1Mpa. The purified air undergoes an oxygen reduction reaction in the cathode chamber 9 to generate pure hydrogen peroxide, which diffuses into the solid electrolyte 13 in the form of HO 2- through the
阴极室9反应方程式如下:O2+H2O+2e-→HO2-+OH- The reaction equation of cathode chamber 9 is as follows: O 2 +H 2 O+2e - →HO 2- +OH -
阴极室9的反应压力与HO2-产率的关系如下表1所示:The relationship between the reaction pressure in the cathode chamber 9 and the HO 2- yield is shown in Table 1 below:
表1Table 1
阳极室14的主要材料为多孔氧化碳纸-钒酸铋复合电极,有效工作面积为100cm2,工作电流密度0.2A/cm2。预纯化水在阳极室14发生水氧化反应,生成H+与纯净过氧化氢(水流速为1000mL/h时过氧化氢产率为1mmol/cm2/h),H+沿阳离子交换膜扩散进入固态电解质13,与来自阴极的HO2-结合生成H2O2,并被水洗出光电催化系统。阳极室14反应方程式如下:2H2O→H2O2+2(H++e-)The main material of the anode chamber 14 is a porous carbon oxide paper-bismuth vanadate composite electrode, the effective working area is 100 cm 2 , and the working current density is 0.2 A/cm 2 . The prepurified water undergoes water oxidation reaction in the anode chamber 14 to generate H + and pure hydrogen peroxide (the hydrogen peroxide yield is 1 mmol/cm 2 /h when the water flow rate is 1000 mL/h), and H + diffuses along the cation exchange membrane and enters The solid electrolyte 13, combines with HO 2- from the cathode to generate H 2 O 2 and is washed out of the photoelectric catalytic system by water. The reaction equation of the anode chamber 14 is as follows: 2H 2 O→H 2 O 2 +2(H + +e − )
特别地,通过外接可见光源15辐照,阳极室14能够将光能转化为光电子,光电子在偏压下来到阴极室9,参与生成H2O2。反应压力为1MPa,水流速为1000mL/h时,可见光光源15功率与阴极室H2O2产率的关系如下表2所示:In particular, by being irradiated by an external visible light source 15, the anode chamber 14 can convert light energy into photoelectrons, and the photoelectrons go to the cathode chamber 9 under a bias voltage to participate in the generation of H 2 O 2 . When the reaction pressure is 1MPa and the water flow rate is 1000mL/h, the relationship between the power of the visible light source 15 and the H 2 O 2 yield in the cathode chamber is shown in Table 2 below:
表2Table 2
通过改变供水流速,能够得到不同质量分数的过氧化氢水溶液。在200W光照下,所收集的H2O2质量分数与水流速的关系如下表3所示:By changing the flow rate of water supply, hydrogen peroxide aqueous solutions of different mass fractions can be obtained. Under 200W illumination, the relationship between the mass fraction of H2O2 collected and the water flow rate is shown in Table 3 below:
表3table 3
优选地,进气管路上的空气流经气体流速阀8调节后以100mL/min的流速进入光电催化系统。其中,固态电解质13的材料可以为苯乙烯-二乙烯苯共聚物,厚度为0.5cm。采用固态电解质能够最大限度地避免反应介质对过氧化氢纯度、性状的影响,例如:液态反应介质容易引入杂质,提高除杂难度,增加成本;液态介质的pH值影响过氧化氢的稳定性等。Preferably, the air flow on the intake pipeline enters the photoelectric catalytic system at a flow rate of 100 mL/min after being adjusted by the gas flow rate valve 8 . Wherein, the material of the solid electrolyte 13 may be styrene-divinylbenzene copolymer with a thickness of 0.5 cm. The use of solid electrolyte can minimize the influence of the reaction medium on the purity and properties of hydrogen peroxide. For example, the liquid reaction medium is easy to introduce impurities, which increases the difficulty of removing impurities and increases the cost; the pH value of the liquid medium affects the stability of hydrogen peroxide, etc. .
优选地,水氧净化系统的供水流速为10~1000mL/h,空气泵6的压力为20kPa,供气流速为100mL/minPreferably, the water supply flow rate of the water and oxygen purification system is 10-1000mL/h, the pressure of the air pump 6 is 20kPa, and the air supply flow rate is 100mL/min
本发明工作原理大概如下:自来水经电磁阀1,通过水压机2增压进入纯化柱3并预纯化,预纯化水在流速阀控制下以不同流速(10~1000mL/h)经过电磁阀5进入催化系统。进气通路上依次设置有空气泵6,滤网7和流速阀8,空气经空气泵6增压,通过滤网7得到纯化空气,经流速阀8调节,最终以100mL/min的流速进入光电催化系统。通过调节光电催化系统的阴极室9内气体流入与流出比,从而调制阴极室9的工作压力0~1MPa。纯化空气在阴极室9发生氧还原反应,生成纯净过氧化氢,过氧化氢以HO2-的形式经过阴离子交换膜16扩散进入固态电解质13,与来自阳极的H+离子结合生成H2O2,之后被水洗出催化系统。多余空气由阴极室9的另一端经止回阀10、出风口11流出。预纯化水在阳极室14发生水氧化反应,生成纯净过氧化氢和H+,过氧化氢被洗出阳极室14,而H+沿阳离子交换膜17扩散进入固态电解质13,与HO2-结合形成H2O2。通过改变阴极室9反应压力、供水流速、阳极室14光照功率,能够得到不同质量分数(1~30wt.%)的过氧化氢水溶液。生成的过氧化氢经检测器18检测产品质量后,流入储罐19备用。储罐19中的过氧化氢经加压泵20流入水流电磁阀21,在水流电磁阀21的一端流出设备,得到高纯过氧化氢;高纯过氧化氢经水流电磁阀21的另一端进入精化柱22,流出设备,得到超高纯过氧化氢。The working principle of the present invention is roughly as follows: the tap water passes through the solenoid valve 1, is pressurized by the hydraulic press 2 and enters the purification column 3 and is pre-purified. system. An air pump 6, a filter screen 7 and a flow rate valve 8 are arranged on the intake passage in turn. The air is pressurized by the air pump 6, and purified air is obtained through the filter screen 7, adjusted by the flow rate valve 8, and finally enters the photoelectric with a flow rate of 100mL/min. catalytic system. By adjusting the gas inflow and outflow ratio in the cathode chamber 9 of the photocatalytic system, the working pressure of the cathode chamber 9 is adjusted to 0-1 MPa. The purified air undergoes an oxygen reduction reaction in the cathode chamber 9 to generate pure hydrogen peroxide, which diffuses into the solid electrolyte 13 in the form of HO 2- through the
采用本发明的一体化装置生产得到的过氧化氢规格为:高纯过氧化氢水溶液(有机碳总含量≤20ppm,各类金属杂质总量≤200ppb,颗粒(≥0.5μm)(个/mL)≤25,过氧化氢总含量1~30wt.%),超高纯过氧化氢水溶液(有机碳总含量≤10ppm,各类金属杂质总量≤2ppb,颗粒(≥0.2μm)(个/mL)≤5,过氧化氢总含量1~30wt.%)。The specifications of hydrogen peroxide produced by the integrated device of the present invention are: high-purity hydrogen peroxide aqueous solution (total organic carbon content ≤ 20 ppm, total amount of various metal impurities ≤ 200 ppb, particles (≥ 0.5 μm) (pieces/mL) ≤25, total hydrogen peroxide content 1~30wt.%), ultra-high purity hydrogen peroxide aqueous solution (total organic carbon content ≤10ppm, total amount of various metal impurities ≤2ppb, particles (≥0.2μm) (pieces/mL) ≤5, the total content of hydrogen peroxide is 1~30wt.%).
以上所述仅是本发明的优选应用实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred application embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the technical principles of the present invention, several improvements and modifications can be made. These improvements and Retouching should also be regarded as the protection scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110316197.XA CN115198288A (en) | 2021-03-24 | 2021-03-24 | Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110316197.XA CN115198288A (en) | 2021-03-24 | 2021-03-24 | Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115198288A true CN115198288A (en) | 2022-10-18 |
Family
ID=83570412
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110316197.XA Pending CN115198288A (en) | 2021-03-24 | 2021-03-24 | Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115198288A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115676933A (en) * | 2022-11-11 | 2023-02-03 | 泉州南京大学环保产业研究院 | A water surface mobile algae removal method |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101392386A (en) * | 2008-10-23 | 2009-03-25 | 上海交通大学 | Electrochemical method for the simultaneous production of sodium chlorate and alkaline hydrogen peroxide |
CN101748422A (en) * | 2008-12-19 | 2010-06-23 | 中国科学院大连化学物理研究所 | Method for preparing alkaline hydrogen peroxide in situ |
JP2016089250A (en) * | 2014-11-10 | 2016-05-23 | 国立研究開発法人産業技術総合研究所 | Light energy utilization method and light energy utilization apparatus |
CN105970247A (en) * | 2016-07-19 | 2016-09-28 | 李国岭 | Monocrystal semiconductor oxide anode and electrolytic cell for preparing hydrogen peroxide |
CN107313068A (en) * | 2016-04-26 | 2017-11-03 | 中国科学院大连化学物理研究所 | A kind of electrochemical method of synthetic acidic hydrogen peroxide |
CN108439346A (en) * | 2018-01-19 | 2018-08-24 | 河海大学常州校区 | Corona discharge pulse water mist synthesizes hydrogen peroxide plant design and parameter regulates and controls method |
CN111472016A (en) * | 2020-04-15 | 2020-07-31 | 中南大学 | A kind of method for preparing hydrogen peroxide by electrolytic recovery of sodium sulfate waste liquid |
-
2021
- 2021-03-24 CN CN202110316197.XA patent/CN115198288A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101392386A (en) * | 2008-10-23 | 2009-03-25 | 上海交通大学 | Electrochemical method for the simultaneous production of sodium chlorate and alkaline hydrogen peroxide |
CN101748422A (en) * | 2008-12-19 | 2010-06-23 | 中国科学院大连化学物理研究所 | Method for preparing alkaline hydrogen peroxide in situ |
JP2016089250A (en) * | 2014-11-10 | 2016-05-23 | 国立研究開発法人産業技術総合研究所 | Light energy utilization method and light energy utilization apparatus |
CN107313068A (en) * | 2016-04-26 | 2017-11-03 | 中国科学院大连化学物理研究所 | A kind of electrochemical method of synthetic acidic hydrogen peroxide |
CN105970247A (en) * | 2016-07-19 | 2016-09-28 | 李国岭 | Monocrystal semiconductor oxide anode and electrolytic cell for preparing hydrogen peroxide |
CN108439346A (en) * | 2018-01-19 | 2018-08-24 | 河海大学常州校区 | Corona discharge pulse water mist synthesizes hydrogen peroxide plant design and parameter regulates and controls method |
CN111472016A (en) * | 2020-04-15 | 2020-07-31 | 中南大学 | A kind of method for preparing hydrogen peroxide by electrolytic recovery of sodium sulfate waste liquid |
Non-Patent Citations (1)
Title |
---|
CHUAN XIA ET AL: "Direct electrosynthesis of pure aqueous H2O2 solutions up to 20% by weight using a solid electrolyte", SCIENCE, vol. 366, no. 6462, 11 October 2019 (2019-10-11), pages 226, XP055801846, DOI: 10.1126/science.aay1844 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115676933A (en) * | 2022-11-11 | 2023-02-03 | 泉州南京大学环保产业研究院 | A water surface mobile algae removal method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2021129566A1 (en) | Device and method for preparing high-purity hydrogen and/or oxygen by electrolyzing water | |
CN217839154U (en) | Hydrogen production and hydrogenation integrated system | |
CN103130307A (en) | Ozone and photo-electrochemical coupled oxidation water-treatment device and method | |
CN201296697Y (en) | Integrated ozone/electrochemical treatment device for organic wastewater | |
CN115198288A (en) | Integrated device and method for producing high-purity hydrogen peroxide by water-oxygen photoelectrocatalysis | |
CN116874043A (en) | Electrochemical double-membrane reactor and wastewater treatment method based on electrochemical double-membrane reactor | |
CN105712555A (en) | Resource utilization method of high-salinity organic wastewater formed in light stabilizer 944 production | |
CN216073399U (en) | A low temperature plasma sewage treatment device | |
CN114920400A (en) | Treatment process method and system for preparing ultrapure water from urban reclaimed water | |
CN111905739B (en) | Preparation method of catalyst applied to oxygen generator | |
CN110642340B (en) | Circulating flow type electric-assisted ozone water treatment equipment and method for treating water by using same | |
CN211226612U (en) | Integrated treatment device for removing hydrogen sulfide from landfill leachate | |
CN217479241U (en) | Treatment process system for preparing ultrapure water from urban reclaimed water | |
CN213231883U (en) | Device for treating wastewater based on physical adsorption coupling photo-Fenton oxidation technology | |
CN116589073A (en) | In situ simultaneous production of O 3 And H 2 O 2 Advanced oxidation reactor and process | |
CN206417949U (en) | Refuse leachate film concentrates liquid treating system | |
CN214141733U (en) | Wastewater treatment device for generating H2O2 in situ by utilizing O3 tail gas in water treatment | |
CN104591351B (en) | A kind of electrolysis with ion-exchange film slot device of processing chemical production wastewater | |
CN115140878A (en) | System and method for producing hydrogen peroxide with low energy consumption and removing perfluorinated compounds in water in situ | |
CN209098291U (en) | A kind of device of ozone and the processing of electrochemistry concerted catalysis oxidized waste water | |
CN217298032U (en) | Integrated portable device for hydrogen peroxide in-situ production | |
CN101481156A (en) | Pressurized light-catalyzed reaction system | |
CN206476851U (en) | A kind of recycling recycling and processing device containing golden electroplating wastewater | |
CN207347666U (en) | A kind of energy saving peak valley hydrogen preparation system | |
CN220913920U (en) | Tritium removal and purified water preparation device of electrolytic coupling hydrogen fuel cell device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination |