TWI571326B - Composite metal oxide electrode structure and manufacturing method thereof - Google Patents
Composite metal oxide electrode structure and manufacturing method thereof Download PDFInfo
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- 229910044991 metal oxide Inorganic materials 0.000 title claims description 83
- 150000004706 metal oxides Chemical class 0.000 title claims description 83
- 239000002131 composite material Substances 0.000 title claims description 67
- 238000004519 manufacturing process Methods 0.000 title claims description 17
- 229910052751 metal Inorganic materials 0.000 claims description 83
- 239000002184 metal Substances 0.000 claims description 83
- 239000002689 soil Substances 0.000 claims description 69
- 239000007769 metal material Substances 0.000 claims description 62
- 239000010410 layer Substances 0.000 claims description 49
- 238000005067 remediation Methods 0.000 claims description 46
- 238000000034 method Methods 0.000 claims description 33
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 30
- 230000005520 electrodynamics Effects 0.000 claims description 23
- 238000006243 chemical reaction Methods 0.000 claims description 20
- 239000000463 material Substances 0.000 claims description 20
- 229910052782 aluminium Inorganic materials 0.000 claims description 19
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 19
- 230000015556 catabolic process Effects 0.000 claims description 16
- 238000006731 degradation reaction Methods 0.000 claims description 16
- 239000002957 persistent organic pollutant Substances 0.000 claims description 16
- 239000012792 core layer Substances 0.000 claims description 15
- 230000003647 oxidation Effects 0.000 claims description 15
- 238000007254 oxidation reaction Methods 0.000 claims description 15
- 230000007246 mechanism Effects 0.000 claims description 12
- 239000000356 contaminant Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 229910052742 iron Inorganic materials 0.000 claims description 10
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 8
- 230000002269 spontaneous effect Effects 0.000 claims description 8
- 239000007791 liquid phase Substances 0.000 claims description 5
- 230000033116 oxidation-reduction process Effects 0.000 claims description 5
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 230000033558 biomineral tissue development Effects 0.000 claims description 2
- 238000005554 pickling Methods 0.000 claims description 2
- 238000010276 construction Methods 0.000 claims 1
- 239000000460 chlorine Substances 0.000 description 8
- 239000010802 sludge Substances 0.000 description 7
- 239000005416 organic matter Substances 0.000 description 6
- 238000006479 redox reaction Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 229910001385 heavy metal Inorganic materials 0.000 description 4
- 238000011065 in-situ storage Methods 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 230000005684 electric field Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- HEFNNWSXXWATRW-UHFFFAOYSA-N Ibuprofen Chemical compound CC(C)CC1=CC=C(C(C)C(O)=O)C=C1 HEFNNWSXXWATRW-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000000593 degrading effect Effects 0.000 description 2
- 238000005370 electroosmosis Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229960001680 ibuprofen Drugs 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229930195730 Aflatoxin Natural products 0.000 description 1
- XWIYFDMXXLINPU-UHFFFAOYSA-N Aflatoxin G Chemical compound O=C1OCCC2=C1C(=O)OC1=C2C(OC)=CC2=C1C1C=COC1O2 XWIYFDMXXLINPU-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 239000005409 aflatoxin Substances 0.000 description 1
- KCZFLPPCFOHPNI-UHFFFAOYSA-N alumane;iron Chemical compound [AlH3].[Fe] KCZFLPPCFOHPNI-UHFFFAOYSA-N 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
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- 238000004070 electrodeposition Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001089 mineralizing effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000271 synthetic detergent Substances 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
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Description
本發明係關於一種複合金屬氧化電極構造及其製造方法用於土壤整治;特別是關於一種鐵鋁〔Al/Fe〕複合金屬氧化電極構造及其製造方法;更特別是關於一種長效型〔long-acting〕複合金屬氧化電極構造及其製造方法適用於處理有機污染物〔organic contamination〕,例如:布洛芬〔IBU,ibuprofen〕。 The invention relates to a composite metal oxide electrode structure and a manufacturing method thereof for soil remediation; in particular to an iron-aluminum [Al/Fe] composite metal oxide electrode structure and a manufacturing method thereof; more particularly, a long-acting type [long] -acting] The composite metal oxide electrode structure and its manufacturing method are suitable for treating organic pollutants such as ibuprofen [Ibuprofen].
有關習用電動力土壤整治裝置,例如:中華民國專利第M377425號〝環境電動力技術之中空透水性電極棒結構〞之新型專利案,其揭示一種中空透水性電極棒結構,其包含:一電場裝置使預設區域內之土壤產生電場,其具有一正極及一負極;至少二電極棒分別設於各該正、負極上,該電極棒呈中空桿狀,其中央以軸線方向形成一空間,並以徑向穿設之至少一滲孔,為可連通該空間至電極棒外徑緣之通孔;利用各該電極棒分別設於各該正極及負極上,當產生電場時,土壤內之陰離子開始朝向正極游移;重金屬陽離子及溶解在水中之有機物則皆朝向負極游移,並可滲入至該空間內以集中,可方便於配合一抽出裝置將該空間內之重金屬污染物予以抽出。 A novel patent for a conventional electric power soil remediation device, for example, a hollow water-permeable electrode rod structure of the environmental electric power technology of the Republic of China Patent No. M377425, which discloses a hollow water-permeable electrode rod structure comprising: an electric field device An electric field is generated in the soil in the predetermined area, and has a positive electrode and a negative electrode; at least two electrode rods are respectively disposed on each of the positive and negative electrodes, and the electrode rod has a hollow rod shape, and a center thereof forms a space in the axial direction, and The at least one perforation hole radially penetrated is a through hole that can connect the space to the outer diameter edge of the electrode rod; and each of the electrode rods is respectively disposed on each of the positive electrode and the negative electrode, and an anion in the soil when an electric field is generated Beginning to move toward the positive electrode; heavy metal cations and organic matter dissolved in water migrate toward the negative electrode and can penetrate into the space for concentration, which can be easily extracted by a withdrawal device to remove heavy metal contaminants in the space.
另一習用電動力土壤整治裝置,例如:中華民國專利第I249441號〝電動力整治重金屬污染土壤之系統與方法〞之發明專利案,其揭示一種電動力整治系統與其 方法。電動力反應槽為開放式,將不同寬度之子槽可置入該電動力反應槽內,可供作土壤子槽、緩衝子槽、電極區等。 Another conventional electric power soil remediation device, for example, the system and method for rectifying heavy metal contaminated soil by the electric power of the Republic of China Patent No. I249441, which discloses an electrodynamic remediation system and method. The electrodynamic reaction tank is open, and sub-grooves of different widths can be placed in the electrodynamic reaction tank, and can be used as a soil sub-tank, a buffer sub-tank, an electrode area, and the like.
另一習用電動力土壤整治裝置,例如:中華民國專利第I408258號〝電動力法採用雙金屬氧化物電極之再生系統〞之發明專利案,其揭示一種電動力法採用雙金屬氧化物電極之再生系統。該再生系統包含一電源裝置、一陰極及一陽極。該電源裝置用以供應電動力移除污染物之所需電力至該陰極及陽極。該陰極電性連接於該電源裝置,且該陰極連接一待再生元件之一第一端。該陽極電性連接於該電源裝置,且該陽極連接該待再生元件之一第二端,以便自該待再生元件進行電動力移除污染物。該陽極係屬一雙金屬氧化電極,如此該雙金屬氧化電極在該陽極進行污染物降解。 Another conventional electric power soil remediation device, for example, the Republic of China Patent No. I408258, the electric power method using a double metal oxide electrode regeneration system, the invention patent case, which discloses an electrodynamic method using a double metal oxide electrode for regeneration system. The regeneration system includes a power supply unit, a cathode, and an anode. The power supply unit is configured to supply electric power to remove the required power of the contaminants to the cathode and the anode. The cathode is electrically connected to the power supply device, and the cathode is connected to a first end of a component to be regenerated. The anode is electrically connected to the power supply device, and the anode is connected to a second end of the component to be regenerated to electrically remove contaminants from the component to be regenerated. The anode is a double metal oxide electrode such that the double metal oxide electrode undergoes contaminant degradation at the anode.
另一習用電動力土壤整治裝置,例如:中華民國專利第I280952號〝改善土壤〔污泥〕鉛、銅含量之方法〞之發明專利案,其揭示一種改善土壤〔污泥〕鉛、銅含量之方法可維持pH中性,且具提升去除土壤〔污泥〕重金屬效率。將陽、陰二電極設置在操作液儲存槽中,且不與土壤〔污泥〕直接接觸,並對處理土壤〔污泥〕施加一直流電壓。 Another conventional electrodynamic soil remediation device, for example, the Republic of China Patent No. I280952, a method for improving the lead and copper content of soil [sludge], discloses an invention patent case, which discloses an improvement of soil (sludge) lead and copper content. The method can maintain pH neutrality and improve the efficiency of removing heavy metals from soil [sludge]. The anode and cathode electrodes are placed in the operating fluid storage tank, and are not in direct contact with the soil [sludge], and a DC voltage is applied to the treated soil [sludge].
另一習用電動力土壤整治裝置,例如:中華民國專利第293056號〝被污染非均質土壞之原位補救〞之發明專利案,其揭示一種被污染非均質土壤區域之原位補救方法。該原位補救方法包含〔a〕將處理被污染非均質土壞區域中污染物之物質投入至少該被污染非均質土壤區域中一液體可滲透區域,以於該被污染非均質土壤區域中形成一處理區,〔b〕傳導直接電流通過被污染非均質土壤區域中至少一低滲透性土壤區,介於第一電極和具有相反電荷 之第二電極之間,其中〔i〕第一電極位在被污染非均質土壤區域之首端,而第二電極則位於被污染非均質土壤區域之相對端或〔ii〕第一電極位在每個低滲透性土壤區域之首端,及第二電極位在每個低滲透性土壤區域之相對端,〔1〕以造成一種由第二電極至第一電極之電滲透流,〔2〕造成一種離子污染物朝相反電荷電極方向的電遷移移動,或〔3〕造成一種由第二電極至第一電極的電滲透流及一種離子污染物朝相反電荷電極方向的電遷移移動,並且〔c〕應用一種橫過被污染非均質土壤區域之水壓降,以造成一種由被污染非均質土壤區域之高壓端至被污染非均質土壤區域之低壓端的水壓流。 Another conventional electrodynamic soil remediation device, such as the Republic of China Patent No. 293056, invented in situ remediation of contaminated heterogeneous soil, discloses an in situ remediation method for contaminated heterogeneous soil regions. The in-situ remedy method comprises [a] introducing a substance for treating pollutants in a bad area of the contaminated heterogeneous soil into at least one liquid permeable region of the contaminated heterogeneous soil region to form in the contaminated heterogeneous soil region. a treatment zone, [b] conducting a direct current through at least one low permeability soil zone in the contaminated heterogeneous soil zone, between the first electrode and having opposite charges Between the second electrodes, wherein [i] the first electrode is at the head end of the contaminated heterogeneous soil region, and the second electrode is at the opposite end of the contaminated heterogeneous soil region or [ii] the first electrode is at The first end of each low permeability soil region, and the second electrode position at the opposite end of each low permeability soil region, [1] to cause an electroosmotic flow from the second electrode to the first electrode, [2] Causing an electromigration movement of an ionic contaminant toward the opposite charge electrode, or [3] causing an electroosmotic flow from the second electrode to the first electrode and an electromigration movement of an ionic contaminant toward the opposite charge electrode, and c] Applying a water pressure drop across the contaminated heterogeneous soil region to create a water pressure flow from the high pressure end of the contaminated heterogeneous soil region to the low pressure end of the contaminated heterogeneous soil region.
另外,關於習用電動力土壤整治技術,其亦揭示於許多國外專利,例如:中國專利公告第102527707號、美國專利第6193867號及美國專利公開第2006163068號申請案。前述專利及專利申請案僅為本發明技術背景之參考及說明目前技術發展狀態而已,其並非用以限制本發明之範圍。 In addition, regarding the conventional electrodynamic soil remediation technology, it is also disclosed in many foreign patents, for example, Chinese Patent Publication No. 102527707, U.S. Patent No. 6,193,867, and U.S. Patent Application Publication No. 2006163068. The above-mentioned patents and patent applications are merely for the purpose of the technical background of the present invention and are not intended to limit the scope of the present invention.
事實上,前述中華民國專利第M377425號、第I249441號、中國專利公告第102527707號及美國專利第6193867號為僅屬採用傳統式惰性電極進行電動力整治土壤技術而已。然而,傳統式惰性電極亦僅能移除污染物部分而已,即其仍具有無法有效進行全面土壤整治的技術問題。 In fact, the aforementioned Republic of China Patent Nos. M377425, No. I249441, Chinese Patent Publication No. 102527707, and U.S. Patent No. 6,193,867 are only those which employ conventional inert electrodes for electrodynamic remediation of soil technology. However, the conventional inert electrode can only remove the contaminant portion, that is, it still has technical problems that cannot effectively perform overall soil remediation.
另外,前述中華民國專利公告第I408258號採用複合金屬氧化電極,即採用改良式之雙金屬氧化物電極及其再生系統。然而,許多複合金屬電極通常為選擇由貴重金屬製成,因此其仍具有製造成本價格較昂貴及較不符合經濟效益之技術前題。 In addition, the aforementioned Republic of China Patent Publication No. I408258 employs a composite metal oxide electrode, that is, an improved double metal oxide electrode and a regeneration system thereof. However, many composite metal electrodes are typically made of precious metals, so they still have the technical premise that manufacturing costs are relatively expensive and less economical.
另外,前述中華民國專利公告第I280952號之 改善土壤〔污泥〕鉛、銅含量之方法及第293056號之被污染非均質土壤區域之補救方法僅為被污染土壤的一般修護技術方法而已,其仍具有無法有效進行全面整治土壤的技術問題。 In addition, the aforementioned Republic of China Patent Notice No. I280952 The method for improving the lead and copper content of soil [sludge] and the remedy for contaminated heterogeneous soil area No. 293056 are only general repair techniques for contaminated soil, and there are still technologies that cannot effectively remediate the soil. problem.
有鑑於此,本發明為了滿足上述技術問題及需求,其提供一種複合金屬氧化電極構造、其用於土壤整治方法及其製造方法,其於一氧化電極設置一複合金屬層,而該複合金屬層包含一第一金屬材料及一第二金屬材料,且利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生一自發反應,以便該第一金屬材料〔例如:鋁或含鋁材料〕可供應電子,以利該第二金屬材料之氧化第二金屬還原形成零價第二金屬〔例如:鐵或含鐵材料〕,再於水中進行芬頓反應,因此相對於習用電動力土壤整治裝置之電極大幅提升其土壤整治效率及降低土壤整治成本之功效。 In view of the above, in order to meet the above technical problems and needs, the present invention provides a composite metal oxide electrode structure, a method for the same, and a method for manufacturing the same, wherein a composite metal layer is disposed on an oxidation electrode, and the composite metal layer is provided. And comprising a first metal material and a second metal material, and utilizing the oxidation-reduction potential of the first metal material and the second metal material to appropriately generate a spontaneous reaction, so that the first metal material (for example, aluminum or aluminum-containing material) An electron can be supplied to reduce the oxidation of the second metal material to form a zero-valent second metal (for example, iron or a ferrous material), and then perform a Fenton reaction in water, thereby comparing the conventional electrodynamic soil remediation device The electrode greatly enhances the efficiency of soil remediation and reduces the cost of soil remediation.
本發明較佳實施例之主要目的係提供一種複合金屬氧化電極構造、其用於土壤整治方法及其製造方法,其於一氧化電極設置一複合金屬層,而該複合金屬層包含一第一金屬材料及一第二金屬材料,且利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生一自發反應,以便該第一金屬材料〔例如:鋁或含鋁材料〕可供應電子,以利該第二金屬材料之氧化第二金屬還原形成零價第二金屬〔例如:鐵或含鐵材料〕,再於水中進行芬頓反應,以達成土壤整治效率及降低土壤整治成本之目的。 The main object of the preferred embodiment of the present invention is to provide a composite metal oxide electrode structure for use in a soil remediation method and a method for fabricating the same, wherein a composite metal layer is disposed on an oxidation electrode, and the composite metal layer comprises a first metal a material and a second metal material, and utilizing the oxidation-reduction potential of the first metal material and the second metal material to appropriately generate a spontaneous reaction, so that the first metal material (for example, aluminum or an aluminum-containing material) can supply electrons to The second metal of the second metal material is reduced to form a zero-valent second metal (for example, iron or a ferrous material), and then subjected to a Fenton reaction in water to achieve soil remediation efficiency and reduce soil remediation costs.
為了達成上述目的,本發明較佳實施例之複合金屬氧化電極用於土壤整治方法包含:將一金屬氧化電極由一第一金屬材料及一第二金屬材料製成; 利用該金屬氧化電極形成為一陽極,且該金屬氧化電極用於電動力土壤整治;在進行電動力土壤整治時,利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生一自發反應,以便該第一金屬材料可供應電子,以利該第二金屬材料之氧化第二金屬還原形成零價第二金屬;及再於水中進行芬頓反應,以便進行降解或礦化一有機污染物。 In order to achieve the above object, a composite metal oxide electrode according to a preferred embodiment of the present invention is used for a soil remediation method comprising: forming a metal oxide electrode from a first metal material and a second metal material; The metal oxide electrode is formed as an anode, and the metal oxide electrode is used for electrodynamic soil remediation; in the electrodynamic soil remediation, a spontaneous reaction is appropriately generated by using the redox potential of the first metal material and the second metal material So that the first metal material can supply electrons, so that the second metal of the second metal material is reduced to form a zero-valent second metal; and the Fenton reaction is further performed in water to degrade or mineralize an organic pollutant. .
本發明較佳實施例之該金屬氧化電極為一圓柱體或一扁柱體。 In the preferred embodiment of the invention, the metal oxide electrode is a cylinder or a flat cylinder.
本發明較佳實施例之該第一金屬材料設置於一電極芯層,而該第二金屬材料設置於一電極外層。 In a preferred embodiment of the invention, the first metal material is disposed on an electrode core layer, and the second metal material is disposed on an electrode outer layer.
本發明較佳實施例之該第一金屬材料選自鋁或含鋁材料,而該第二金屬材料選自鐵或含鐵材料。 In a preferred embodiment of the invention, the first metallic material is selected from the group consisting of aluminum or an aluminum containing material, and the second metallic material is selected from the group consisting of iron or ferrous materials.
為了達成上述目的,本發明較佳實施例之複合金屬氧化電極構造包含:一金屬氧化電極,其為一陽極,且該金屬氧化電極用於電動力土壤整治;一電極芯層,其由一第一金屬材料製成;及一電極外層,其由一第二金屬材料製成,且該電極外層設置於該電極芯層上;其中該電極芯層及電極外層組成該金屬氧化電極,且利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生一自發反應,以便該第一金屬材料可供應電子,以利該第二金屬材料之氧化第二金屬還原形成零價第二金屬,再於水中進行芬頓反應,以便進行降解或礦化一有機污染物。 In order to achieve the above object, a composite metal oxide electrode structure according to a preferred embodiment of the present invention comprises: a metal oxide electrode which is an anode, and the metal oxide electrode is used for electrodynamic soil remediation; an electrode core layer, which is composed of a metal material; and an electrode outer layer, which is made of a second metal material, and the electrode outer layer is disposed on the electrode core layer; wherein the electrode core layer and the electrode outer layer constitute the metal oxide electrode, and the The redox potential of the first metal material and the second metal material appropriately generates a spontaneous reaction, so that the first metal material can supply electrons, so that the second metal of the second metal material is reduced to form a zero-valent second metal, and then The Fenton reaction is carried out in water to degrade or mineralize an organic contaminant.
本發明較佳實施例之該金屬氧化電極為一圓柱體或一扁柱體。 In the preferred embodiment of the invention, the metal oxide electrode is a cylinder or a flat cylinder.
本發明較佳實施例之該圓柱體或扁柱體組成一電極陣列。 In the preferred embodiment of the invention, the cylinder or the flat cylinder constitutes an electrode array.
本發明較佳實施例之該第一金屬材料選自鋁或含鋁材料,而該第二金屬材料選自鐵或含鐵材料。 In a preferred embodiment of the invention, the first metallic material is selected from the group consisting of aluminum or an aluminum containing material, and the second metallic material is selected from the group consisting of iron or ferrous materials.
本發明較佳實施例之該電極外層為一複合第二金屬層,且該複合第二金屬層包含數個第二金屬層。 In the preferred embodiment of the invention, the outer layer of the electrode is a composite second metal layer, and the composite second metal layer comprises a plurality of second metal layers.
為了達成上述目的,本發明較佳實施例之複合金屬氧化電極製造方法包含:將至少一第一金屬棒進行酸洗,並取出該第一金屬棒;將該第一金屬棒浸漬於一第二金屬離子溶液,並取出該第一金屬棒;將該第一金屬棒進行預先烘乾;及將該第一金屬棒進行高溫烘烤鍛燒,以便在該第一金屬棒上形成至少一第二金屬層。 In order to achieve the above object, a composite metal oxide electrode manufacturing method according to a preferred embodiment of the present invention comprises: pickling at least one first metal rod, and taking out the first metal rod; immersing the first metal rod in a second a metal ion solution, and taking out the first metal rod; pre-baking the first metal rod; and subjecting the first metal rod to high temperature baking and calcining to form at least one second on the first metal rod Metal layer.
本發明較佳實施例之該第一金屬選自鋁或含鋁材料,而該第二金屬選自鐵或含鐵材料。 In a preferred embodiment of the invention, the first metal is selected from the group consisting of aluminum or an aluminum-containing material, and the second metal is selected from the group consisting of iron or a ferrous material.
本發明較佳實施例在該第二金屬層形成另一第二金屬層,以便形成一複合第二金屬層。 In a preferred embodiment of the invention, another second metal layer is formed in the second metal layer to form a composite second metal layer.
1‧‧‧金屬氧化電極 1‧‧‧Metal Oxidation Electrode
1’‧‧‧金屬氧化電極 1'‧‧‧Metal Oxidation Electrode
10‧‧‧電極芯層 10‧‧‧electrode core
20‧‧‧電極外層 20‧‧‧ electrode outer layer
第1圖:本發明較佳實施例之複合金屬氧化電極用於土壤整治方法之流程示意圖。 Fig. 1 is a schematic view showing the flow of a composite metal oxide electrode according to a preferred embodiment of the present invention for a soil remediation method.
第2圖:本發明第一較佳實施例之複合金屬氧化電極構造之立體示意圖。 Fig. 2 is a perspective view showing the structure of a composite metal oxide electrode according to a first preferred embodiment of the present invention.
第3圖:本發明第一較佳實施例之複合金屬氧化電極構造在進行氧化還原反應時電子傳導狀態之示意圖。 Fig. 3 is a view showing the state of electron conduction in the case of performing a redox reaction in the composite metal oxide electrode structure of the first preferred embodiment of the present invention.
第4圖:本發明第二較佳實施例之複合金屬氧化電極構造之立體示意圖。 Fig. 4 is a perspective view showing the structure of a composite metal oxide electrode according to a second preferred embodiment of the present invention.
第5圖:本發明第二較佳實施例之複合金屬氧化電極構造組成電極陣列之立體示意圖。 Fig. 5 is a perspective view showing the configuration of an electrode array of a composite metal oxide electrode according to a second preferred embodiment of the present invention.
第6圖:本發明較佳實施例之複合金屬氧化電極於不含Cl-環境下對有機物降解機制之示意圖。 Figure 6 is a schematic view showing the mechanism of degradation of organic matter in a composite metal oxide electrode according to a preferred embodiment of the present invention in a Cl - free environment.
第7圖:本發明較佳實施例之複合金屬氧化電極於含Cl-環境下對有機物降解機制之示意圖。 Figure 7 is a schematic view showing the mechanism of degradation of organic matter in a composite metal oxide electrode according to a preferred embodiment of the present invention in a Cl - containing environment.
第8圖:本發明較佳實施例之複合金屬氧化電極製造方法之流程示意圖。 Figure 8 is a flow chart showing a method of manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention.
為了充分瞭解本發明,於下文將舉例較佳實施例並配合所附圖式作詳細說明,且其並非用以限定本發明。 In order to fully understand the present invention, the preferred embodiments of the present invention are described in detail below, and are not intended to limit the invention.
本發明較佳實施例之複合金屬氧化電極構造及其用於土壤整治方法適用於各種電動力土壤〔污泥〕整治裝置,例如:電動力土壤現場〔in-situ〕整治裝置,但其並非用以限制本發明之範圍。另外,本發明較佳實施例之本發明較佳實施例之複合金屬氧化電極構造、其製造方法及其用於土壤整治方法適用於整治處理污染物為各種有機污染物,但其並非用以限定本發明之應用範圍。 The composite metal oxide electrode structure of the preferred embodiment of the present invention and the method for the soil remediation are applicable to various electrodynamic soil (sludge) remediation devices, for example, an electro-dynamic soil site in-situ remediation device, but it is not used To limit the scope of the invention. In addition, the composite metal oxide electrode structure of the preferred embodiment of the present invention, the manufacturing method thereof and the method for the soil remediation are suitable for remediation of pollutants as various organic pollutants, but it is not limited thereto. The scope of application of the present invention.
一般而言,有機污染物係有機化合物進入環境後,可造成污染環境事件或發生危害人體事件。有機污染物通常依其來源大致可分為天然有機污染物及人工合成有機污染物。天然有機污染物主要為自然化學反應或生物體代謝所產生的各種有害於人體健康、污染環境的有機化合物,例如:黃曲黴素、萜烯、氨基甲酸乙酯等。人工合成有機污染物為由現代化工業生產的各類有機合成物,例如:染料、洗滌劑、有機農藥、塑料、酚類、氰化物、石油、合成洗滌劑等。 In general, organic pollutants, when organic compounds enter the environment, can cause environmental pollution incidents or human events. Organic pollutants are generally classified into natural organic pollutants and synthetic organic pollutants according to their sources. Natural organic pollutants are mainly organic compounds that are harmful to human health and pollute the environment caused by natural chemical reactions or biological metabolism, such as aflatoxin, terpenes, urethane and the like. Synthetic organic pollutants are various organic compounds produced by modern industries, such as dyes, detergents, organic pesticides, plastics, phenols, cyanides, petroleum, synthetic detergents, etc.
第1圖揭示本發明較佳實施例之複合金屬氧化電極用於土壤整治方法之流程示意圖,其大致包含四個步 驟,但其並非用以限定本發明之範圍。請參照第1圖所示,本發明較佳實施例之複合金屬氧化電極用於土壤整治方法包含第一步驟S1:首先,將一金屬氧化電極選擇由一第一金屬材料及一第二金屬材料製成。舉例而言,該金屬氧化電極可選擇製成各種形狀體,且該金屬氧化電極可選擇製成各種結構體,例如:第一金屬層及第二金屬層之交替排列層體或同心圓長條體。該第一金屬材料選自鋁〔Al〕或含鋁元素材料,而該第二金屬材料選自鐵〔Fe〕或含鐵元素材料,以便形成一Fe/Al複合金屬氧化電極。 1 is a schematic flow chart showing a method for using a composite metal oxide electrode for soil remediation according to a preferred embodiment of the present invention, which comprises substantially four steps. However, it is not intended to limit the scope of the invention. Referring to FIG. 1 , a composite metal oxide electrode for use in a soil remediation method according to a preferred embodiment of the present invention includes a first step S1: first, a metal oxide electrode is selected from a first metal material and a second metal material. production. For example, the metal oxide electrode can be selected into various shapes, and the metal oxide electrode can be selected into various structures, for example, alternating layers or concentric strips of the first metal layer and the second metal layer. body. The first metal material is selected from aluminum [Al] or an aluminum-containing material, and the second metal material is selected from iron [Fe] or an iron-containing material to form an Fe/Al composite metal oxide electrode.
請再參照第1圖所示,本發明較佳實施例之複合金屬氧化電極用於土壤整治方法包含第二步驟S2:接著,利用該金屬氧化電極形成為一陽極〔anode〕或一正極,且該金屬氧化電極用於電動力土壤整治。舉例而言,該金屬氧化電極之陽極對應於一陰極〔cathode〕或一負極,以形成一電動力土壤整治系統,且該陰極由其它金屬〔例如,不鏽鋼〕製成。 Referring to FIG. 1 again, the composite metal oxide electrode according to the preferred embodiment of the present invention is used in a soil remediation method comprising a second step S2: then, using the metal oxide electrode to form an anode or a positive electrode, and The metal oxide electrode is used for electrodynamic soil remediation. For example, the anode of the metal oxide electrode corresponds to a cathode or a negative electrode to form an electrodynamic soil remediation system, and the cathode is made of other metals such as stainless steel.
請再參照第1圖所示,本發明較佳實施例之複合金屬氧化電極用於土壤整治方法包含第三步驟S3:接著,在進行電動力土壤整治時,在該陽極上利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生一自發反應〔spontaneous reaction〕,以便該第一金屬材料可供應電子〔e-〕,以利該第二金屬材料之氧化第二金屬〔例如:氧化鐵〕還原形成零價第二金屬。 Referring to FIG. 1 again, the composite metal oxide electrode of the preferred embodiment of the present invention is used in a soil remediation method comprising a third step S3: then, in the electrodynamic soil remediation, the first metal is utilized on the anode The redox potential of the material and the second metal material suitably generates a spontaneous reaction such that the first metal material can supply electrons [e - ] to facilitate oxidation of the second metal material to the second metal [eg, oxidation Iron] is reduced to form a zero-valent second metal.
請再參照第1圖所示,本發明較佳實施例之複合金屬氧化電極用於土壤整治方法包含第四步驟S4:接著,再於水中進行芬頓〔Fenton〕反應,以便進行降解〔attenuation〕或礦化〔mineralization〕一有機污染物。如此有機污染物多數能在環境中被降解成簡單無機物,其降解形成對人體無害的產物。 Referring to FIG. 1 again, the composite metal oxide electrode of the preferred embodiment of the present invention is used in a soil remediation method comprising a fourth step S4: followed by a Fenton reaction in water for degradation (attenuation). Or mineralization of an organic pollutant. Most of these organic pollutants can be degraded into simple inorganic substances in the environment, and their degradation forms products that are harmless to the human body.
請再參照第1圖所示,本發明利用氧化降解機制包含電極產生之氫氧自由基〔hydroxyl radical〕及操作流質產生之高氧化物〔例如:OCl-〕。舉例而言,本發明利用Fenton反應產生氫氧自由基,並利用氫氧自由基與有機污染物質產生氧化還原反應,以降解或礦化污染物。本發明利用具高氧化能力陰離子之OCl-,以降解有機污染物質,其氧化還原電位如下:2Al0→2Al3++6e- △E=+1.66v Referring to FIG. 1 again, the present invention utilizes an oxidative degradation mechanism to include a hydroxyl radical generated by an electrode and a high oxide (eg, OCl − ) produced by an operating fluid. For example, the present invention utilizes a Fenton reaction to generate hydroxyl radicals and utilizes hydroxyl radicals to generate redox reactions with organic pollutants to degrade or mineralize contaminants. The invention utilizes OCl - with high oxidizing ability anion to degrade organic pollutants, and its oxidation-reduction potential is as follows: 2Al 0 → 2Al 3+ + 6e - △ E = +1.66v
3Fe2++6e-→3Fe0 △E=+0.33v 3Fe 2+ +6e - →3Fe 0 △E=+0.33v
2Al0+3Fe2+→2Al3++3Fe0↓ △E=+1.99v 2Al 0 +3Fe 2+ →2Al 3+ +3Fe 0 ↓ △E=+1.99v
第2圖揭示本發明第一較佳實施例之複合金屬氧化電極構造之立體示意圖。請參照第2圖所示,本發明較佳實施例之複合金屬氧化電極構造包含一金屬氧化電極1、一電極芯層〔electrode core〕10及一電極外層〔electrode shell layer〕20,而該電極芯層10由該第一金屬材料製成,且該電極外層20由該第二金屬材料製成。即該第一金屬材料配置於該電極芯層10,而該第二金屬材料設置於該電極外層20。 Fig. 2 is a perspective view showing the structure of a composite metal oxide electrode according to a first preferred embodiment of the present invention. Referring to FIG. 2, the composite metal oxide electrode structure of the preferred embodiment of the present invention comprises a metal oxide electrode 1, an electrode core 10 and an electrode shell layer 20, and the electrode The core layer 10 is made of the first metal material, and the electrode outer layer 20 is made of the second metal material. That is, the first metal material is disposed on the electrode core layer 10, and the second metal material is disposed on the electrode outer layer 20.
請再參照第2圖所示,舉例而言,該金屬氧化電極1為一圓柱體〔cylinder〕或其它斷面形狀長條體〔elongated rod〕,例如:多角形斷面長條體或齒輪形斷面長條體,且該電極外層20對應設置於該電極芯層10上,以便在該電極芯層10及電極外層20之間形成一氧化還原反應區域。 Referring to FIG. 2 again, for example, the metal oxide electrode 1 is a cylinder or an elongated rod, for example, a polygonal section elongated body or a gear shape. The electrode strip outer layer 20 is correspondingly disposed on the electrode core layer 10 to form a redox reaction region between the electrode core layer 10 and the electrode outer layer 20.
第3圖揭示本發明第一較佳實施例之複合金屬氧化電極構造在進行氧化還原反應時電子傳導狀態之示意圖,其對應於第2圖。請參照第2及3圖所示,該電極芯層10及電極外層20組成該金屬氧化電極1,且利用該第一金屬材料及第二金屬材料之氧化還原電位適當產生自發 反應,以便該第一金屬材料可供應電子〔e-〕,如第3圖之箭頭方向所示,以利該第二金屬材料之氧化第二金屬還原形成零價第二金屬,再於水中進行芬頓反應,以便進行降解或礦化一有機污染物。 Fig. 3 is a view showing the state of electron conduction of the composite metal oxide electrode structure of the first preferred embodiment of the present invention in the redox reaction, which corresponds to Fig. 2. Referring to FIGS. 2 and 3, the electrode core layer 10 and the electrode outer layer 20 constitute the metal oxide electrode 1, and the spontaneous reaction is appropriately generated by the oxidation-reduction potential of the first metal material and the second metal material, so that the first A metal material can supply electrons [e - ] as indicated by the direction of the arrow in Fig. 3, so that the second metal of the second metal material is reduced to form a zero-valent second metal, and then the Fenton reaction is carried out in water. Degrading or mineralizing an organic pollutant.
第4圖揭示本發明第二較佳實施例之複合金屬氧化電極構造之立體示意圖,其對應於第2圖。請參照第4圖所示,相對於第一實施例,本發明第二較佳實施例之金屬氧化電極1’包含一電極芯層10及一電極外層20,且該金屬氧化電極1’為一扁柱體,以便增加在該電極芯層10及電極外層20之間形成一氧化還原反應區域。 Fig. 4 is a perspective view showing the structure of a composite metal oxide electrode according to a second preferred embodiment of the present invention, which corresponds to Fig. 2. Referring to FIG. 4, the metal oxide electrode 1' of the second preferred embodiment of the present invention comprises an electrode core layer 10 and an electrode outer layer 20, and the metal oxide electrode 1' is a first embodiment. A flat cylinder is formed to increase a redox reaction region between the electrode core layer 10 and the electrode outer layer 20.
第5圖揭示本發明第二較佳實施例之複合金屬氧化電極構造組成電極陣列之立體示意圖,其對應於第4圖。請參照第5圖所示,選擇將數個該金屬氧化電極1’以一預定排列間距組成一扁柱體電極陣列,以便依不同需求配置不同數量的該金屬氧化電極1’,且可容置於一電動力土壤現場整治裝置或一電動力土壤整治槽內。 Fig. 5 is a perspective view showing the composite electrode array of the composite metal oxide electrode according to the second preferred embodiment of the present invention, which corresponds to Fig. 4. Referring to FIG. 5, a plurality of the metal oxide electrodes 1' are selected to form a flat cylindrical electrode array at a predetermined arrangement pitch, so as to configure different numbers of the metal oxide electrodes 1' according to different requirements, and can be accommodated. In an electrodynamic soil site remediation device or an electrodynamic soil remediation tank.
請再參照第2及5圖所示,同樣的,選擇將數個該金屬氧化電極1以一預定排列間距組成一圓柱體電極陣列,且該圓柱體電極陣列或扁柱體電極陣列可選擇排列形成各種形狀的電極陣列。或,本發明另一較佳實施例可選擇將數個該金屬氧化電極1及數個該金屬氧化電極1’混合編排形成一混編電極陣列。 Referring to FIGS. 2 and 5 again, in the same manner, a plurality of the metal oxide electrodes 1 are selected to form a cylindrical electrode array at a predetermined arrangement pitch, and the cylindrical electrode array or the flat cylindrical electrode array may be selectively arranged. An array of electrodes of various shapes is formed. Alternatively, another preferred embodiment of the present invention may optionally combine a plurality of the metal oxide electrodes 1 and a plurality of the metal oxide electrodes 1' to form a hybrid electrode array.
第6圖揭示本發明較佳實施例之複合金屬氧化電極於不含Cl-環境下對有機物降解機制之示意圖。請參照第6圖所示,舉例而言,電化學液相降解之處理機制在不含氯之環境下,其降解之主要機制來自於Fe/Al複合金屬氧化電極本身,因產生氫氧自由基可將污染物降解如下式:於陽極2H2O2→O2(g)+4H++4e- Figure 6 is a schematic view showing the mechanism of degradation of organic matter in a composite metal oxide electrode according to a preferred embodiment of the present invention in a Cl-free environment. Please refer to Figure 6, for example, the treatment mechanism of electrochemical liquid phase degradation in the absence of chlorine, the main mechanism of its degradation comes from the Fe / Al composite metal oxide electrode itself, due to the generation of hydroxyl radicals The pollutants can be degraded as follows: at the anode 2H 2 O 2 →O 2 (g)+4H + +4e -
於陰極2H2O2+2e-→H2(g)↑+2OH- At the cathode 2H 2 O 2 +2e - → H 2 (g) ↑ + 2OH -
2Al0→2Al3++6e- 2Al 0 →2Al 3+ +6e -
Fe3++e-→Fe2+ Fe 3+ +e - →Fe 2+
3Fe2++6e-→3Fe0 3Fe 2+ +6e - →3Fe 0
(O2)ads+e-→O2-.或HO2. (O 2 ) ads +e - →O 2- . or HO 2 .
HO2.+HO2.→H2O2+O2 HO 2 . +HO 2 . →H 2 O 2 +O 2
O2-.+O2-.+2H+→H2O2+O2 O 2- .+O 2- .+2H + →H 2 O 2 +O 2
3Fe2++6e-→3Fe0 3Fe 2+ +6e - →3Fe 0
Fe2++H2O2→HO.+OH-+Fe3+ Fe 2+ +H 2 O 2 →HO.+OH - +Fe 3+
Fe3++H2O2→HO2. Fe 3+ + H 2 O 2 → HO 2 .
有機物+HO.→降解化合物 Organic matter + HO. → Degradation compound
第7圖揭示本發明較佳實施例之複合金屬氧化電極於含Cl-環境下對有機物降解機制之示意圖,其對應於第6圖。請參照第7圖所示,舉例而言,電化學液相降解之處理機制在含氯之環境下,其降解之主要機制來自於Fe/Al複合金屬氧化電極本身,因產生氫氧自由基可將污染物降解,亦另可產生具高氧化能力之OCl-,以降解有機污染物質如下式:2Cl-→Cl2+2e- Fig. 7 is a view showing the mechanism of degradation of organic matter by a composite metal oxide electrode in a Cl-containing environment according to a preferred embodiment of the present invention, which corresponds to Fig. 6. Please refer to Figure 7. For example, the treatment mechanism of electrochemical liquid phase degradation in the chlorine-containing environment, the main mechanism of its degradation comes from the Fe/Al composite metal oxide electrode itself, due to the generation of hydroxyl radicals. Degrading contaminants, and also producing OCl - with high oxidizing ability to degrade organic pollutants as follows: 2Cl - → Cl 2 + 2e -
2e-+2H2O→2OH-+H2 2e - +2H 2 O→2OH - +H 2
2OH-+Cl2→Cl-+OCl-+2H2O 2OH - +Cl 2 →Cl - +OCl - +2H 2 O
第8圖揭示本發明較佳實施例之複合金屬氧化電極製造方法之流程示意圖。請參照第8圖所示,本發明較佳實施例之複合金屬氧化電極製造方法包含第一步驟S1:首先,將至少一第一金屬棒〔例如:直徑為5mm、長度為10cm之鋁棒〕以一酸性溶液〔例如:稀釋硫酸溶液〕進行酸洗一預定時間〔例如:約為6分鐘〕,並取出該第一金屬棒。 Figure 8 is a flow chart showing a method of manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention. Referring to FIG. 8, the method for manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention comprises a first step S1: first, at least one first metal rod (for example, an aluminum rod having a diameter of 5 mm and a length of 10 cm) The acid is washed with an acidic solution (for example, a diluted sulfuric acid solution) for a predetermined time (for example, about 6 minutes), and the first metal rod is taken out.
請再參照第8圖所示,本發明較佳實施例之複 合金屬氧化電極製造方法包含第二步驟S2:接著,將該第一金屬棒浸漬於一第二金屬離子溶液〔例如:濃度約1.7M之FeCl3溶液〕一預定時間,並取出該已浸漬第一金屬棒。 Referring to FIG. 8 again, the method for manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention comprises a second step S2: subsequently, immersing the first metal rod in a second metal ion solution (for example, a concentration of about 1.7) The FeCl 3 solution of M is taken for a predetermined time, and the impregnated first metal rod is taken out.
請再參照第8圖所示,本發明較佳實施例之複合金屬氧化電極製造方法包含第三步驟S3:接著,將該已浸漬第一金屬棒以一預定溫度〔約105℃〕進行預先烘乾一預定時間〔例如:約10分鐘〕,以獲得該已烘乾第一金屬棒。 Referring to FIG. 8 again, the method for manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention comprises a third step S3: subsequently, the impregnated first metal rod is pre-baked at a predetermined temperature [about 105 ° C]. Dry for a predetermined time (for example: about 10 minutes) to obtain the dried first metal rod.
請再參照第8圖所示,本發明較佳實施例之複合金屬氧化電極製造方法包含第四步驟S4:接著,將該已烘乾第一金屬棒以一預定溫度〔約500至600℃〕進行高溫烘烤鍛燒一預定時間〔例如:約1至10分鐘〕,以便在該第一金屬棒上形成至少一第二金屬層。本發明另一較佳實施例可選擇將該第一金屬棒以一預定溫度〔約500至600℃〕進行最後高溫烘烤鍛燒一預定時間〔例如:約60分鐘〕。 Referring to FIG. 8 again, the method for manufacturing a composite metal oxide electrode according to a preferred embodiment of the present invention comprises a fourth step S4: subsequently, drying the first metal rod at a predetermined temperature [about 500 to 600 ° C] The high temperature baking is performed for a predetermined time (for example, about 1 to 10 minutes) to form at least one second metal layer on the first metal rod. In another preferred embodiment of the present invention, the first metal bar may be subjected to a final high temperature baking and calcination at a predetermined temperature [about 500 to 600 ° C] for a predetermined time (for example, about 60 minutes).
或,本發明另一較佳實施例可選擇重複第一步驟S1至第四步驟S4數次〔例如:10次〕。在該第二金屬層形成另一第二金屬層,以便形成一複合第二金屬層。最後,可選擇將該第一金屬棒以一預定溫度〔約500至600℃〕進行最後高溫烘烤鍛燒一預定時間〔例如:約60分鐘〕。如此,該電極外層20為一複合第二金屬層,且該複合第二金屬層包含數個第二金屬層,如第2及4圖所示。 Alternatively, another preferred embodiment of the present invention may optionally repeat the first step S1 to the fourth step S4 several times (for example, 10 times). Another second metal layer is formed on the second metal layer to form a composite second metal layer. Finally, the first metal bar may be subjected to a final high temperature baking and calcination at a predetermined temperature [about 500 to 600 ° C] for a predetermined time (for example, about 60 minutes). As such, the electrode outer layer 20 is a composite second metal layer, and the composite second metal layer includes a plurality of second metal layers, as shown in FIGS. 2 and 4.
前述較佳實施例僅舉例說明本發明及其技術特徵,該實施例之技術仍可適當進行各種實質等效修飾及/或替換方式予以實施;因此,本發明之權利範圍須視後附申請專利範圍所界定之範圍為準。本案著作權限制使用於中華民國專利申請用途。 The foregoing preferred embodiments are merely illustrative of the invention and the technical features thereof, and the techniques of the embodiments can be carried out with various substantial equivalent modifications and/or alternatives; therefore, the scope of the invention is subject to the appended claims. The scope defined by the scope shall prevail. The copyright limitation of this case is used for the purpose of patent application in the Republic of China.
1‧‧‧金屬氧化電極 1‧‧‧Metal Oxidation Electrode
10‧‧‧電極芯層 10‧‧‧electrode core
20‧‧‧電極外層 20‧‧‧ electrode outer layer
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