TW201500592A - Method of removing and recycling conductive substrate from carbon layer - Google Patents

Method of removing and recycling conductive substrate from carbon layer Download PDF

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TW201500592A
TW201500592A TW102121762A TW102121762A TW201500592A TW 201500592 A TW201500592 A TW 201500592A TW 102121762 A TW102121762 A TW 102121762A TW 102121762 A TW102121762 A TW 102121762A TW 201500592 A TW201500592 A TW 201500592A
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conductive substrate
electrolyte
carbon layer
graphene
layer
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TW102121762A
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Chinese (zh)
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guo-xing Zhang
Shuo-Fang Zheng
Silva Henry Medina
Si-Ru Pan
You-Ming Lin
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Taiwan Bluestone Technology Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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Abstract

A method of removing and recycling a conductive substrate from a carbon layer comprises electrochemical treatment and wet etching treatment. The electrochemical treatment provides electrolyte, conductor as the cathode and a workpiece to be treated which comprises a conductive substrate as the anode and a carbon layer adhered on the conductive substrate. When the conductive substrate and the conductor are in contact with the electrolyte, electric energy is provided to the conductor and the workpiece to be treated so as to electroplate a part of the conductive substrate onto the surface of the conductor. The wet etching treatment uses etchant to remove residual conductive substrate on the carbon layer to obtain the carbon layer. The method of this invention can not only recycle the conductive substrate but also obtain carbon layer with high quality.

Description

將一導電基層體自一碳層去除及回收的方法 Method for removing and recovering a conductive substrate from a carbon layer

本發明是有關於一種自一含有一導電基層體與一碳層的待處理件去除及回收該導電基層體的方法,特別是指一種結合電化學處理及濕蝕刻處理,而能將一導電基層體自一碳層去除及回收的方法。 The invention relates to a method for removing and recovering the conductive base layer from a workpiece to be processed containing a conductive base layer and a carbon layer, in particular to a conductive base layer combined with electrochemical treatment and wet etching treatment. The method of removing and recovering a body from a carbon layer.

石墨烯由於具有高度撓曲性,且石墨烯的導電度不會因為彎曲捲繞而有任何影響,所以目前非常廣泛地被運用於軟性產品(如軟性顯示器或太陽能板)中。在各種製備石墨烯的方法中,以化學氣相沉積法所製得的石墨烯是形成在一基層體(如金屬層)上,因此,如何將該基層體去除或者如何轉移石墨烯,已成為此領域業者亟欲發展的技術之一。 Graphene is widely used in soft products (such as flexible displays or solar panels) because it has high flexibility and the conductivity of graphene does not have any influence due to bending and winding. In various methods for preparing graphene, graphene prepared by chemical vapor deposition is formed on a substrate (such as a metal layer), so how to remove the substrate or how to transfer graphene has become One of the technologies that industry players are eager to develop.

基層體的去除大多是直接將含有基層體及石墨烯的待處理件浸泡於蝕刻液中,並透過該蝕刻液溶解該基層體而完成基層體的去除;然而此作法會造成基層體的耗損、製程操作時間長,及產生大量的蝕刻廢液造成環境的污染。為了解決前述問題,現今多朝向針對石墨烯的轉移 方法進行研究。 Most of the removal of the substrate is performed by directly immersing the object to be treated containing the substrate and graphene in an etching solution, and dissolving the substrate through the etching solution to complete the removal of the substrate; however, this method causes loss of the substrate, The process time is long, and a large amount of etching waste liquid is generated to cause environmental pollution. In order to solve the aforementioned problems, today's multi-directional transfer to graphene Methods were studied.

Libo Gao等人於2012年在”Nature communication”期刊發表的”Repeated growth and bubbling transfer of graphene with millimetre-size single-crystal grains using platinum”揭示一種用於將鉑基層體及石墨烯分離的電解方法,為一種運用電解產氣方式轉移石墨烯的方法。 "Repeated growth and bubbling transfer of graphene with millimetre-size single-crystal grains using platinum" published by Libo Gao et al., "Nature communication" in 2012, discloses an electrolysis method for separating a platinum-based layer body and graphene. It is a method for transferring graphene by electrolytic gas production.

該方法是提供一氫氧化鈉水溶液、一鉑片(Pt foil),及一包括一鉑基層體及一設置在該鉑基層體上的石墨烯薄膜的待處理件。以該鉑片做為陽極,該鉑基層體做為陰極,並使該鉑片及該鉑基層體接觸氫氧化鈉水溶液,對該鉑片及該鉑基層體施予電能,此時,在該鉑基層體與該石墨烯間產生氫氣,藉由氫氣推擠該石墨烯,使得該石墨烯與該鉑基層體完全分離。 The method provides an aqueous solution of sodium hydroxide, a platinum plate (Pt foil), and a member to be treated comprising a platinum substrate and a graphene film disposed on the platinum substrate. Taking the platinum sheet as an anode, the platinum base layer as a cathode, and contacting the platinum sheet and the platinum base layer with an aqueous sodium hydroxide solution, and applying electric energy to the platinum sheet and the platinum base layer body, at this time, Hydrogen is generated between the platinum base layer and the graphene, and the graphene is pushed by hydrogen to completely separate the graphene from the platinum base layer.

該方法雖能在不耗損鉑基層體的情形下,使石墨烯與鉑基層體完全分離,然而使用該方法所得到的石墨烯,因為氣體推擠石墨烯,會使得石墨烯的完整性被破壞,而造成石墨烯品質不佳。同時,因需要產生足量的氣體,以使石墨烯與鉑基層體完全分離而需要較高的電壓(例如以鉑基層體面積為3 cm2來說,電流密度至少需0.1 A/cm2以上,電壓需求至少為5 V以上,才能產生足量的氣體),造成設備門檻要求及設備成本的增加。且高電壓的操作及大量氫氣及氧氣的產生也會造成操作安全性的問題。此外,在陽極產生的大量氧氣會使陽極發生氧化腐蝕 情形,進而嚴重影響陽極的穩定性。 Although the method can completely separate the graphene from the platinum-based layer body without consuming the platinum-based layer body, the graphene obtained by the method can destroy the integrity of the graphene because the gas pushes the graphene. , resulting in poor quality of graphene. Meanwhile, because of the need to produce sufficient amount of gas, so that the platinum is completely separated from the base layer of the graphene material is required higher voltage (e.g., platinum base layer body area of 3 cm 2, a required current density of at least 0.1 A / cm 2 or more The voltage requirement is at least 5 V to generate a sufficient amount of gas), resulting in an increase in equipment threshold requirements and equipment costs. High voltage operation and the generation of large amounts of hydrogen and oxygen can also cause operational safety problems. In addition, the large amount of oxygen generated at the anode causes oxidative corrosion of the anode, which in turn seriously affects the stability of the anode.

由上述說明可知,透過電解產氣方式轉移石墨烯的方法仍存在各項問題。因此,如何降低轉移過程對石墨烯的損害以獲得一品質良好的石墨烯,同時又可回收基層體,仍為目前業界所欲達成的研發目標。 As apparent from the above description, there are still various problems in the method of transferring graphene by electrolytic gas production. Therefore, how to reduce the damage of graphene during the transfer process to obtain a good quality graphene and at the same time recover the base layer is still the research and development goal that the industry is currently seeking.

因此,本發明之目的,即在提供一種將一導電基層體自一碳層去除及回收的方法,該方法不只能回收基層體且能獲得品質良好的石墨烯。 Accordingly, it is an object of the present invention to provide a method for removing and recovering a conductive substrate from a carbon layer, which method not only recovers the substrate but also obtains graphene of good quality.

於是本發明用以將一導電基層體自一碳層去除及回收的方法,包含:(a)電化學處理,提供一電解液、一導電體,及一待處理件,該待處理件包括一導電基層體,及一附著於該導電基層體上的碳層,且以該導電體做為陰極及該導電基層體做為陽極,將該導電基層體及導電體與該電解液接觸,並對該待處理件及該導電體施予電能,以使部分的該導電基層體電鍍於該導電體表面上;及(b)濕蝕刻處理,以一蝕刻液將殘留在該碳層上的導電基層體去除,以得到該碳層,其中,該蝕刻液可與該電解液相同或不同。 Therefore, the method for removing and recovering a conductive substrate from a carbon layer of the present invention comprises: (a) electrochemically treating, providing an electrolyte, an electrical conductor, and a member to be processed, the workpiece to be processed a conductive base layer, and a carbon layer attached to the conductive base layer, wherein the conductive body is used as a cathode and the conductive base layer is used as an anode, and the conductive base layer and the electrical conductor are in contact with the electrolyte, and The material to be processed and the electrical conductor are energized to partially electroplate the conductive substrate onto the surface of the electrical conductor; and (b) wet etching to deposit a conductive base layer remaining on the carbon layer with an etching solution The body is removed to obtain the carbon layer, wherein the etching solution may be the same as or different from the electrolyte.

本發明之功效在於:在(a)電化學處理及(b)濕蝕刻處理的配合下,不只能回收導電基層體且能得到品質良好的碳層。 The effect of the present invention is that, in combination with (a) electrochemical treatment and (b) wet etching treatment, not only the conductive base layer but also a carbon layer of good quality can be obtained.

以下將就本發明內容進行詳細說明: [步驟(a)的電化學處理]:該步驟(a)的電化學處理的陰極、陽極與電解液間的配置可以依據一般已知方式設置。 The contents of the present invention will be described in detail below: [Electrochemical Treatment of Step (a)]: The arrangement between the electrochemically treated cathode, anode and electrolyte of the step (a) can be set according to a generally known manner.

該導電體的型態可為線狀、棒狀、片狀或網狀等。該導電體的材質於此並無特別限制,只要做為陰極時不與該電解液反應且不會被該電解液溶解,並能於電化學處理時讓部分的導電基層體電鍍於該導電體表面上即可。該導電體的材質例如但不限於:不鏽鋼、石墨、白金、鈦、銥、釕、鉭、氧化釕、氧化銥、銅、鎳、鐵、鋅、銅合金、鎳合金、鐵合金、鋅合金等。上述列舉的材質中,銅、鎳、鐵、鋅、銅合金、鎳合金、鐵合金及鋅合金雖然做為陽極時會溶解於電解液中,但做為陰極時因受陰極的電場保護而不會溶於電解液中,因此也適用於本發明的方法。 The shape of the conductor may be linear, rod, sheet or mesh. The material of the conductor is not particularly limited as long as it does not react with the electrolyte and is not dissolved by the electrolyte, and can partially plate the conductive substrate to the conductor during electrochemical treatment. It can be on the surface. The material of the conductor is, for example but not limited to, stainless steel, graphite, platinum, titanium, niobium, tantalum, niobium, tantalum oxide, niobium oxide, copper, nickel, iron, zinc, a copper alloy, a nickel alloy, an iron alloy, a zinc alloy or the like. Among the materials listed above, copper, nickel, iron, zinc, copper alloy, nickel alloy, iron alloy and zinc alloy are dissolved in the electrolyte when used as an anode, but they are not protected by the electric field of the cathode when used as a cathode. It is soluble in the electrolyte and is therefore also suitable for use in the process of the invention.

該導電基層體的材質於此並無特別限制,只要能於電化學處理時,溶解於該電解液中,並電鍍於該導電體上即可。較佳地,該導電基層體是選自於銅、鎳、鐵、鈷、鋅、銅合金、鎳合金、鐵合金、鈷合金或鋅合金。 The material of the conductive base layer is not particularly limited as long as it can be dissolved in the electrolytic solution during electrochemical treatment and plated on the conductor. Preferably, the conductive substrate is selected from the group consisting of copper, nickel, iron, cobalt, zinc, copper alloys, nickel alloys, iron alloys, cobalt alloys or zinc alloys.

該碳層的材質於此並無別限制,該碳層的材質可單獨或混合使用,例如但不限於:石墨、石墨烯、奈米碳纖維、奈米碳管、富勒烯、類鑽碳(Diamond-Like Carbon,簡稱DLC)等。 The material of the carbon layer is not limited herein, and the material of the carbon layer may be used singly or in combination, such as, but not limited to, graphite, graphene, nano carbon fiber, carbon nanotube, fullerene, diamond-like carbon ( Diamond-Like Carbon, referred to as DLC).

該待處理件還包括一設置於該碳層上的高分子層。該高分子層的材質於此並無特別限制,其同樣不可與 該電解液反應且不會被該電解液溶解。該高分子層的材質可單獨或混合使用,例如但不限於:聚甲基丙烯酸甲酯、聚乙烯醇、聚二甲基矽氧烷、矽膠、乙烯-醋酸乙烯酯樹脂、聚乙烯、聚苯乙烯或聚丙烯。該電解液只要能使部分的該導電基層體電鍍於該導電體表面上即可。該電解液是選自於中性電解液、酸性電解液,或鹼性電解液。該中性電解液能單獨或混合使用,該中性電解液例如但不限於:含鋰鹽的溶液、含鈉鹽的溶液、含鉀鹽的溶液或含銨鹽的溶液等。鋰鹽例如但不限於:硫酸鋰(Li2SO4)、氯化鋰(LiCl)、硝酸鋰(LiNO3)等。鈉鹽例如但不限於:硫酸鈉(Na2SO4)、氯化鈉(NaCl)、硝酸鈉(NaNO3)等。鉀鹽例如但不限於:氯化鉀(KCl)、硫酸鉀(K2SO4)、硝酸鉀(KNO3)等。銨鹽例如但不限於:氯化銨(NH4Cl)、硝酸銨(NH4NO3),或硫酸銨[(NH4)2SO4]等。該酸性電解液例如但不限於:硫酸(H2SO4)溶液、氯化氫(HCl)溶液、過氯酸(HClO4)溶液、磷酸(H3PO4)溶液、碳酸(H2CO3)溶液、過氧化氫(H2O2)溶液或硝酸(HNO3)溶液等。該鹼性電解液包括鹼性電解質、溶劑及螯合劑。因導電基層體的離子在鹼性電解液中會形成氫氧化物鈍化膜或沉澱物,會導致導電基層體無法電鍍於導電體表面,因此當電解液為鹼性電解液時,還需添加該螯合劑以避免上述情況發生。該鹼性電解質能單獨或混合使用,例如但不限於:氫氧化鋰(LiOH)、氫氧化鈉(NaOH)、氫氧化鉀(KOH)或氫氧化銨(NH4OH)等。該螯合劑能單獨或混合使用,例如但不限於:檸檬酸 (citric acid)或乙二胺四乙酸(EDTA)等。該溶劑只要能使該鹼性電解質及該螯合劑溶解即可,該溶劑可單獨或混合使用,例如但不限於水。較佳地,該電解液是酸性電解液。 The workpiece to be processed further includes a polymer layer disposed on the carbon layer. The material of the polymer layer is not particularly limited, and it is also not reactive with the electrolytic solution and is not dissolved by the electrolytic solution. The material of the polymer layer may be used singly or in combination, such as, but not limited to, polymethyl methacrylate, polyvinyl alcohol, polydimethyl siloxane, silicone, ethylene-vinyl acetate resin, polyethylene, polyphenylene. Ethylene or polypropylene. The electrolyte may be such that a part of the conductive substrate is plated on the surface of the conductor. The electrolyte is selected from a neutral electrolyte, an acidic electrolyte, or an alkaline electrolyte. The neutral electrolyte may be used singly or in combination, and the neutral electrolyte may be, for example but not limited to, a lithium salt-containing solution, a sodium salt-containing solution, a potassium salt-containing solution or an ammonium salt-containing solution. The lithium salt is, for example but not limited to, lithium sulfate (Li 2 SO 4 ), lithium chloride (LiCl), lithium nitrate (LiNO 3 ), and the like. The sodium salt is, for example but not limited to, sodium sulfate (Na 2 SO 4 ), sodium chloride (NaCl), sodium nitrate (NaNO 3 ), and the like. Potassium salts are, for example but not limited to, potassium chloride (KCl), potassium sulfate (K 2 SO 4 ), potassium nitrate (KNO 3 ), and the like. The ammonium salt is, for example but not limited to, ammonium chloride (NH 4 Cl), ammonium nitrate (NH 4 NO 3 ), or ammonium sulfate [(NH 4 ) 2 SO 4 ] or the like. The acidic electrolyte is, for example but not limited to, a solution of sulfuric acid (H 2 SO 4 ), a solution of hydrogen chloride (HCl), a solution of perchloric acid (HClO 4 ), a solution of phosphoric acid (H 3 PO 4 ), a solution of carbonic acid (H 2 CO 3 ). , hydrogen peroxide (H 2 O 2 ) solution or nitric acid (HNO 3 ) solution, and the like. The alkaline electrolyte includes an alkaline electrolyte, a solvent, and a chelating agent. Since the ions of the conductive substrate body form a hydroxide passivation film or a precipitate in the alkaline electrolyte, the conductive substrate body cannot be plated on the surface of the conductor, so when the electrolyte is an alkaline electrolyte, it is necessary to add the Chelating agents to avoid this. The alkaline electrolyte can be used singly or in combination, such as, but not limited to, lithium hydroxide (LiOH), sodium hydroxide (NaOH), potassium hydroxide (KOH) or ammonium hydroxide (NH 4 OH). The chelating agent can be used singly or in combination, such as, but not limited to, citric acid or ethylenediaminetetraacetic acid (EDTA). The solvent may be dissolved in the alkaline electrolyte and the chelating agent, and the solvent may be used singly or in combination, such as, but not limited to, water. Preferably, the electrolyte is an acidic electrolyte.

該電解液的pH值範圍為0至14。較佳地,該電解液的pH值範圍為0至6。較佳地,該電解液的濃度範圍為1 mM至6 M。 The pH of the electrolyte ranges from 0 to 14. Preferably, the electrolyte has a pH in the range of 0 to 6. Preferably, the concentration of the electrolyte ranges from 1 mM to 6 M.

[步驟(b)的濕蝕刻處理]:該蝕刻液是依據導電基層體的材質做選擇,只要能使導電基層體蝕刻溶解即可。該蝕刻液能單獨或混合使用,該蝕刻液例如但不限於:銅蝕刻液(例如:Alfa Aesar製的銅蝕刻液,型號:44583)、鎳蝕刻液(例如:BASF製的鎳蝕刻液,型號:NPE-400 EC)等。於電化學處理時,也可使用能導電的蝕刻液做為電解液,以加速電化學處理的速度。 [Wet Etching Treatment of Step (b)]: The etching liquid is selected according to the material of the conductive base layer, as long as the conductive base layer can be etched and dissolved. The etching solution can be used singly or in combination, and the etching liquid is, for example but not limited to, a copper etching solution (for example, a copper etching solution made by Alfa Aesar, model: 44583), a nickel etching solution (for example, a nickel etching solution made of BASF, model number). : NPE-400 EC) and so on. In the electrochemical treatment, an electrically conductive etching solution can also be used as the electrolyte to accelerate the speed of the electrochemical treatment.

於本發明用以將一導電基層體自一碳層去除及回收的方法中,先利用(a)電化學處理,透過使部分的該導電基層體電鍍於該導電體表面上而得以回收導電基層體,再利用(b)濕蝕刻處理將殘留在該碳層上的導電基層體去除而得以得到碳層。本發明的方法,在(a)電化學處理的階段不需高操作電壓,更無損碳層的品質,再配合(b)濕蝕刻處理,而能回收導電基層體並得到品質良好的碳層。 In the method for removing and recovering a conductive substrate from a carbon layer in the present invention, the conductive substrate is recovered by (a) electrochemical treatment by partially plating the conductive substrate onto the surface of the conductive body. The carbon layer is obtained by removing the conductive substrate remaining on the carbon layer by (b) wet etching. The method of the present invention can recover the conductive base layer and obtain a good quality carbon layer without (b) high operating voltage, non-destructive quality of the carbon layer, and (b) wet etching treatment.

本發明將就以下實施例來作進一步說明,但應瞭解的是,該實施例僅為例示說明之用,而不應被解釋為本發明實施之限制。 The present invention will be further illustrated by the following examples, but it should be understood that this embodiment is intended to be illustrative only and not to be construed as limiting.

<實施例><Example> [實施例1][Example 1] 《電化學處理》 Electrochemical Treatment

提供一電解液(Alfa Aesar製的銅蝕刻液,商品型號:44583)、一導電體[材質:二氧化釕,面積:3cm×5cm,此時的重量記錄為(Wa0)],及一待處理件[此時的重量記錄為重量(Wb0)],該待處理件包括一導電基層體(材質:銅,面積:1cm×3cm)、一以氣相沉積法形成於該導電基層體上且厚度為小於1 nm的石墨烯層,及一形成在該石墨烯層表面的聚甲基丙烯酸酯層。 Providing an electrolyte (copper etching solution made by Alfa Aesar, product model number: 44583), an electric conductor [material: cerium oxide, area: 3 cm × 5 cm, the weight recorded at this time is (W a0 )], and waiting for The processing member [the weight at this time is recorded as the weight (W b0 )], and the to-be-processed member includes a conductive base layer (material: copper, area: 1 cm × 3 cm), and is formed on the conductive substrate by vapor deposition. And a graphene layer having a thickness of less than 1 nm, and a polymethacrylate layer formed on the surface of the graphene layer.

以該導電體做為陰極,該導電基層體做為陽極,將該導電體及該導電基層體接觸該電解液,並對該導電體及該導電基層體施予一電能(電壓:1.2 V,電流:0.2 A,電流密度:67 mA/cm2,功率:0.24 W)[施予電能時記為電化學處理的起始時間(t0)],此時會有部分的導電基層體逐漸溶解於該電解液中,並電鍍於該導電體的表面上。當電流大幅下降時(電流:0.01 A),停止供應電能[停止供應電能時記為電化學處理的結束時間(t1)],並量測此時導電體的重量(Wa1),及待處理件的重量(Wb1)。 Taking the electric conductor as a cathode, the conductive base layer is used as an anode, the electric conductor and the conductive base layer are in contact with the electrolyte, and an electrical energy is applied to the electric conductor and the conductive base layer (voltage: 1.2 V, Current: 0.2 A, current density: 67 mA/cm 2 , power: 0.24 W) [When the electrical energy is applied, it is recorded as the starting time (t 0 ) of the electrochemical treatment], at which time some of the conductive substrate gradually dissolves. In the electrolyte, and electroplated on the surface of the electrical conductor. When the current drops significantly (current: 0.01 A), the supply of electric energy is stopped [the end time (t 1 ) of the electrochemical treatment is stopped when the electric energy is stopped], and the weight (W a1 ) of the electric conductor at this time is measured, and The weight of the treatment piece (W b1 ).

《濕蝕刻處理》 Wet Etching Treatment

將經過上述電化學處理的待處理件從電解液中移出後,移至一蝕刻液(Alfa Aesar製的銅蝕刻液,商品型號:44583)中[移至蝕刻液中時記為濕蝕刻處理的起始時間(t2)],此時該蝕刻液會逐漸將殘留在該石墨烯層上的導電基層體去除,待蝕刻液將導電基層體完全去除後[導電基層體完全去除時記為濕蝕刻處理的結束時間(t3)],即得到該石墨烯層。 After the electrochemically treated material to be processed is removed from the electrolyte, it is transferred to an etching solution (copper etching solution manufactured by Alfa Aesar, product model number: 44583). [When it is transferred to an etching solution, it is recorded as wet etching. Starting time (t 2 )], at this time, the etching liquid gradually removes the conductive base layer remaining on the graphene layer, and the etching liquid layer completely removes the conductive base layer body [when the conductive base layer body is completely removed, it is recorded as wet The graphene layer was obtained by the end time (t 3 ) of the etching treatment.

[實施例2至5][Examples 2 to 5]

實施例2至5是以與實施例1相同的方法進行,差別在於使用不同的電解液及電能條件。其中,實施例2至5所使用的電解液為硫酸水溶液(濃度:0.5 M,表1中記為硫酸(aq.)),蝕刻液為銅蝕刻液(Alfa Aesar製的銅蝕刻液,商品型號:44583)。 Examples 2 to 5 were carried out in the same manner as in Example 1, except that different electrolytes and electric energy conditions were used. The electrolyte used in Examples 2 to 5 was an aqueous solution of sulfuric acid (concentration: 0.5 M, which is referred to as sulfuric acid (aq.) in Table 1), and the etching solution was a copper etching solution (copper etching solution manufactured by Alfa Aesar, product type) :44583).

上述實施例1至5所使用的電解液及蝕刻液種類,及電能條件是由表1所示。 The types of the electrolytic solution and the etching liquid used in the above Examples 1 to 5, and the electric energy conditions are shown in Table 1.

[比較例1]濕蝕刻法[Comparative Example 1] Wet etching method

提供一待處理件,該待處理件是與實施例1中的待處理件相同,故不再贅述。將該待處理件與一蝕刻液(Alfa Aesar製的銅蝕刻液,商品型號:44583)接觸,進行一濕蝕刻處理[記為濕蝕刻處理的起始時間t4],待蝕刻液將導電基層體完全去除後[記為濕蝕刻處理的結束時間(t5)],即得到該石墨烯層。 A member to be processed is provided, which is the same as the member to be processed in Embodiment 1, and therefore will not be described again. The workpiece to be treated is brought into contact with an etching solution (copper etching solution manufactured by Alfa Aesar, product model number: 44583), and subjected to a wet etching treatment (referred to as a starting time t 4 of the wet etching treatment), and the etching solution is to be a conductive substrate. After the body is completely removed [indicated as the end time (t 5 ) of the wet etching treatment], the graphene layer is obtained.

[比較例2]電解產氣轉移法[Comparative Example 2] Electrolytic gas transfer method

提供一氫氧化鈉水溶液做為電解液(濃度:1 M,表1中記為氫氧化鈉(aq.))、一導電體[材質:二氧化釕,面積:3cm×5cm],及一待處理件,該待處理件是與實施例1中的待處理件相同,故不再贅述。 Providing an aqueous solution of sodium hydroxide as an electrolyte (concentration: 1 M, denoted as sodium hydroxide (aq.) in Table 1), an electric conductor [material: cerium oxide, area: 3 cm × 5 cm], and The processing member is the same as the member to be processed in Embodiment 1, and therefore will not be described again.

以該導電體做為陽極,該待處理件的導電基層體做為陰極,將該導電體及該導電基層體接觸該電解液,並對該導電體及該導電基層體施予一電能(電壓:10 V,電流:15 A,電流密度:500 mA/cm2,功率:150 W)[施予電能時記為電解產氣轉移法的起始時間(t6)],此時會有氣泡於導電體及導電基層體處產生,而使石墨烯層與導電基層體完全分離[石墨烯層與導電基層體完全分離時記為電解產氣轉移法的結束時間(t7)]。 Taking the electric conductor as an anode, the conductive base layer of the to-be-processed member serves as a cathode, the electric conductor and the conductive base layer are in contact with the electrolyte, and an electric energy (voltage is applied to the electric conductor and the conductive base layer) : 10 V, current: 15 A, current density: 500 mA/cm 2 , power: 150 W) [When the electric energy is applied, it is recorded as the start time (t 6 ) of the electrolytic gas transfer method], and there are bubbles at this time. It is produced at the conductor and the conductive substrate, and the graphene layer is completely separated from the conductive substrate [when the graphene layer and the conductive substrate are completely separated, it is referred to as the end time (t 7 ) of the electrolytic gas transfer method].

[評價項目][evaluation project]

1.操作時間 Operation time

依據下式(1)計算,即得到實施例1至5的操作時間,單位:min.。 According to the following formula (1), the operation time of the examples 1 to 5 is obtained, and the unit is min.

實施例1至5的操作時間=(t1-t0)+(t3-t2) 式(3) Operation time of Examples 1 to 5 = (t 1 - t 0 ) + (t 3 - t 2 ) Equation (3)

依據下式(2)計算,即得到比較例1的操作時間,單位:min.。 Calculated according to the following formula (2), the operation time of Comparative Example 1 was obtained, and the unit was min.

比較例1的操作時間=(t5-t4) 式(2) Operation time of Comparative Example 1 = (t 5 - t 4 ) Equation (2)

依據下式(3)計算,即得到比較例2的操作時間,單位:min.。 Calculated according to the following formula (3), the operation time of Comparative Example 2 was obtained, and the unit was min.

比較例2的操作時間=(t7-t6) 式(3) Operation time of Comparative Example 2 = (t 7 - t 6 ) Equation (3)

2.回收率 2. Recovery rate

依據下式(4)計算,即得到實施例1至5的回收 率,單位:%。 According to the following formula (4), the recovery of Examples 1 to 5 is obtained. Rate, unit: %.

回收率=(Wa1-Wa0)÷(Wb0-Wb1)×100% 式(4) Recovery rate = (W a1 - W a0 ) ÷ (W b0 - W b1 ) × 100% Equation (4)

3.石墨烯層的片電阻值 3. Sheet resistance of graphene layer

將實施例1至5及比較例1至2方法所得到的石墨烯層,利用四點探針量測儀(廠商:Jandel型號:RM3000)量測石墨烯層的片電阻值,每一石墨烯層取10點數據的平均值。石墨烯層的片電阻值為700 ohm/cm2以下,可視為品質優良。 The graphene layers obtained in the methods of Examples 1 to 5 and Comparative Examples 1 to 2 were measured for sheet resistance of the graphene layer by a four-point probe measuring instrument (manufacturer: Jandel model: RM3000), each graphene The layer takes the average of 10 points of data. The sheet resistance of the graphene layer is 700 ohm/cm 2 or less, which can be regarded as excellent in quality.

上述各評價項目的結果由表1所示。 The results of the above evaluation items are shown in Table 1.

由表1的結果可知,相較於比較例1的濕蝕刻法完全無法回收導電基層體,實施例1至5的方法的導電基層體回收率能達到61%至97%,更值得一提的是,實施例1至5的方法所得到的石墨烯層仍具有良好的品質(片電阻值510至660 ohm/cm2)。且相較於比較例1的濕蝕刻法,實施例1及3至5的方法的操作時間更是大幅縮短至11至 18分鐘。 As can be seen from the results of Table 1, the conductive substrate was completely incapable of being recovered by the wet etching method of Comparative Example 1, and the recovery of the conductive substrate of the methods of Examples 1 to 5 was 61% to 97%, which is more worth mentioning. Yes, the graphene layers obtained by the methods of Examples 1 to 5 still have good quality (sheet resistance value 510 to 660 ohm/cm 2 ). Moreover, the operation time of the methods of Examples 1 and 3 to 5 was greatly shortened to 11 to 18 minutes as compared with the wet etching method of Comparative Example 1.

比較例2電解產氣轉移法得到的石墨烯層的片電阻值高達1170 ohm/cm2,可見電解產氣轉移法的確會嚴重地損害石墨烯層的品質,相較之下,實施例1至5的方法所得到的石墨烯層則具有優良的品質。此外,相較於比較例2的電解產氣轉移法需要較高的電壓(10V),實施例1至5的方法的電壓只需0.4 V至1.6 V,進而能避免因高電壓操作會產生的安全性及設備需求較高的問題。 The sheet resistance of the graphene layer obtained by the electrolytic gas transfer method of Comparative Example 2 was as high as 1170 ohm/cm 2 , and it was found that the electrolytic gas transfer method did seriously impair the quality of the graphene layer, in contrast, Example 1 to The graphene layer obtained by the method of 5 has excellent quality. In addition, compared with the electrolytic gas transfer method of Comparative Example 2, a higher voltage (10 V) is required, and the voltages of the methods of Embodiments 1 to 5 are only 0.4 V to 1.6 V, thereby avoiding the occurrence of high voltage operation. The problem of high security and equipment requirements.

綜上所述,本發明用以將一導電基層體自一碳層去除及回收的方法,在(a)電化學處理及(b)濕蝕刻處理的配合下,不只能回收導電基層體又能得到品質良好的碳層,且操作時無需高電壓,故確實能達成本發明之目的。 In summary, the method for removing and recovering a conductive base layer from a carbon layer of the present invention can not only recover the conductive base layer but also can be recovered by the combination of (a) electrochemical treatment and (b) wet etching treatment. A carbon layer of good quality is obtained, and high voltage is not required for operation, so the object of the present invention can be achieved.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及專利說明書內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。 The above is only the preferred embodiment of the present invention, and the scope of the present invention is not limited thereto, that is, the simple equivalent changes and modifications made by the patent application scope and patent specification content of the present invention, All remain within the scope of the invention patent.

Claims (5)

一種將一導電基層體自一碳層去除及回收的方法,包含:(a)電化學處理,提供一電解液、一導電體,及一待處理件,該待處理件包括一導電基層體,及一附著於該導電基層體上的碳層,且以該導電體做為陰極及該導電基層體做為陽極,將該導電基層體及導電體與該電解液接觸,並對該待處理件及該導電體施予電能,以使部分的該導電基層體電鍍於該導電體表面上;及(b)濕蝕刻處理,以一蝕刻液將殘留在該碳層上的導電基層體去除,以得到該碳層;其中,該電解液與該蝕刻液可為相同或不同。 A method for removing and recovering a conductive substrate from a carbon layer, comprising: (a) electrochemical treatment, providing an electrolyte, an electrical conductor, and a member to be treated, the component to be processed comprising a conductive substrate, And a carbon layer attached to the conductive substrate, and using the electrical conductor as a cathode and the conductive substrate as an anode, contacting the conductive substrate and the electrical conductor with the electrolyte, and the workpiece to be processed And the electrical conductor is energized to partially electroplate the conductive substrate onto the surface of the electrical conductor; and (b) wet etching to remove the conductive substrate remaining on the carbon layer with an etching solution to remove The carbon layer is obtained; wherein the electrolyte and the etching solution may be the same or different. 如請求項1所述的方法,其中,該電解液為酸性電解液。 The method of claim 1, wherein the electrolyte is an acidic electrolyte. 如請求項1所述的方法,其中,該電解液的pH值範圍為0至6。 The method of claim 1, wherein the electrolyte has a pH in the range of 0 to 6. 如請求項1所述的方法,其中,該電解液的濃度範圍為1 mM至6 M。 The method of claim 1, wherein the concentration of the electrolyte ranges from 1 mM to 6 M. 如請求項1所述的方法,其中,該導電基層體是選自於銅、鎳、鐵、鈷、鋅、銅合金、鎳合金、鐵合金、鈷合金或鋅合金。 The method of claim 1, wherein the conductive substrate is selected from the group consisting of copper, nickel, iron, cobalt, zinc, a copper alloy, a nickel alloy, an iron alloy, a cobalt alloy, or a zinc alloy.
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