TW201527600A - Apparatus for graphene formation - Google Patents

Apparatus for graphene formation Download PDF

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TW201527600A
TW201527600A TW103100718A TW103100718A TW201527600A TW 201527600 A TW201527600 A TW 201527600A TW 103100718 A TW103100718 A TW 103100718A TW 103100718 A TW103100718 A TW 103100718A TW 201527600 A TW201527600 A TW 201527600A
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electrode
graphene
porous filler
present
potential difference
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TW103100718A
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TWI585241B (en
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Lain-Jong Li
Feng-Yu Wu
Tzu-Yin Chen
Tung Chou
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Nitronix Nanotechnology Corp
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Abstract

An apparatus for graphene formation is provided. The apparatus includes an electrolytic chamber, at least one first electrode, at least one second electrode, a holder, a graphene formatting material and a porous packing. The electrolytic cell has electrolyte solution. The first electrode is disposed corresponding to the second electrode, and the first and second electrodes are clamped by the holder. The graphene formatting material is disposed on the second electrode, and the porous packing is sandwiched by the first and second electrodes.

Description

石墨烯生成裝置 Graphene generating device

本發明為一種生成裝置,特別是一種石墨烯的生成裝置。 The invention is a generating device, in particular a graphene generating device.

石墨烯(graphene)是一種單層原子厚的碳材料,每個碳原子之間以sp2混成與相鄰的三個原子形成鍵結,並延伸成蜂窩狀的二維結構。且石墨烯的更以良好的載子遷移率(carrier mobility)著稱,因其具有優異的電學性能、化學穩定性、良好的導熱及高穿透率等性質,故石墨烯目前已被廣泛應用於半導體、觸控面板或太陽能電池等領域中的熱門材料。 Graphene is a single layer of atomic carbon material. Each carbon atom is sp 2 mixed with adjacent three atoms and forms a honeycomb two-dimensional structure. Moreover, graphene is more famous for its good carrier mobility. Because of its excellent electrical properties, chemical stability, good thermal conductivity and high transmittance, graphene has been widely used. Popular materials in the fields of semiconductors, touch panels or solar cells.

一般石墨烯的生成方式有機械剝離法(mechanical exfoliation)、磊晶成長法(epitaxial growth)、化學氣相沈積法(chemical vapor deposition,CVD)及化學剝離法(chemical exfoliation)等方法。其中,機械剝離法及磊晶成長法,雖然可以生成品質較佳之石墨烯,但這兩種方法均無法大量合成石墨烯。 Generally, the formation method of graphene includes mechanical exfoliation, epitaxial growth, chemical vapor deposition (CVD), and chemical exfoliation. Among them, the mechanical exfoliation method and the epitaxial growth method can produce graphene with better quality, but neither method can synthesize graphene in a large amount.

且,若採用化學氣相沈積法,其操作溫度為近千度的高溫及昂貴的金屬基板,且製備過程須耗費數小時才能完成。上述這些方法的不足之處,都限制了石墨烯之生產及後續的應用。而化學剝離法則是在強酸、強氧化的條件下,透過將石墨氧化還原的方法生成石墨烯。此作法雖適合大量生產,但其生成的石墨烯的表面結構及大小較不理想。 Moreover, if chemical vapor deposition is used, the operating temperature is near a thousand degrees of high temperature and an expensive metal substrate, and the preparation process takes several hours to complete. The shortcomings of these methods limit the production and subsequent application of graphene. The chemical stripping method produces graphene by redoxing the graphite under strong acid and strong oxidation conditions. Although this method is suitable for mass production, the surface structure and size of the graphene produced are less than ideal.

除了上述的生成方法以外,亦可透過電化學剝離法生成石墨烯。其主要的作用原理為透過電解質與石墨表面的相互作用,使得陽極的石墨材料表層被氧化並剝離。雖習知電化學剝離的方式,無法控制石墨原材料從電極上剝離的程度(可能無法完全剝離),以及無法有效率的應用電解槽的空間。但相較上述其他的生成方法,電化學剝離法能夠快速且經濟地在室溫環境下製造石墨烯,換言之,若能改善化學剝離法生成效率、石 墨烯產量,將能使電化學剝離法成為經濟且大規模製作的石墨烯生成方法。 In addition to the above-described production method, graphene can also be produced by an electrochemical stripping method. Its main principle of action is that the interaction between the electrolyte and the graphite surface causes the surface of the graphite material of the anode to be oxidized and stripped. Although the manner of electrochemical stripping is conventionally controlled, it is impossible to control the extent to which the graphite raw material is peeled off from the electrode (may not be completely peeled off), and the space in which the electrolytic cell cannot be efficiently used. However, compared with the other generation methods described above, the electrochemical stripping method can rapidly and economically produce graphene at room temperature, in other words, if the chemical stripping method can be improved, stone The production of ocene will enable the electrochemical stripping method to be an economical and large-scale production method of graphene.

因此,如何提供一種能於常溫下生產,成本低廉、提升效率及提高整體生產高品質的石墨烯生成裝置,已成為本領域亟需解決的重要課題之一。 Therefore, how to provide a graphene generating device capable of producing at a normal temperature, low in cost, improving efficiency, and improving overall production quality has become one of the important problems to be solved in the field.

有鑑於上述課題,本發明之目的為提供一種可提升石墨烯產量、生成效率以及可量產的石墨烯生成裝置。 In view of the above problems, an object of the present invention is to provide a graphene generating apparatus which can improve graphene production, production efficiency, and mass production.

為達上述目的,依據本發明可提供一種石墨烯生成裝置,包括電解槽、夾具、至少一第一電極、至少一第二電極、石墨烯材料以及多孔填充材。 To achieve the above object, according to the present invention, there is provided a graphene generating apparatus comprising an electrolytic cell, a jig, at least a first electrode, at least a second electrode, a graphene material, and a porous filler.

電解槽得以填充電解液,至少一第二電極與第一電極相對設置。且夾具夾置第一電極與第二電極。石墨烯材料可設置於第二電極。多孔填充材可設置於第一電極以及第二電極之間。 The electrolytic cell is filled with the electrolyte, and at least one second electrode is disposed opposite to the first electrode. And the clamp sandwiches the first electrode and the second electrode. The graphene material may be disposed on the second electrode. The porous filler may be disposed between the first electrode and the second electrode.

在一實施例中,更包括電源供應器,分別與第一電極與第二電極電性連接,並使第一電極與第二電極產生一電勢差。 In an embodiment, the power supply is further connected to the first electrode and the second electrode, respectively, and the first electrode and the second electrode generate a potential difference.

在一實施例中,第一電極與第二電極具有電勢差,且電勢差介於5伏特至100伏特之間。 In an embodiment, the first electrode and the second electrode have a potential difference and the potential difference is between 5 volts and 100 volts.

在一實施例中,電勢差更可介於10伏特至50伏特之間。 In an embodiment, the potential difference may be between 10 volts and 50 volts.

在一實施例中,更包括濾網,設置於多孔填充材與石墨烯材料之間。 In one embodiment, a screen is further included between the porous filler and the graphene material.

在一實施例中,多孔填充材的孔徑大小介於5μm至1mm之間。 In an embodiment, the porous filler has a pore size between 5 μm and 1 mm.

在一實施例中,其中多孔填充材為多孔陶瓷板、海綿、發泡塑膠、塑膠網、沸石、石英綿或其組合。 In one embodiment, the porous filler material is a porous ceramic plate, a sponge, a foamed plastic, a plastic mesh, a zeolite, a quartz sponge, or a combination thereof.

在一實施例中,第一電極及第二電極為石墨材料或金屬所製成。 In an embodiment, the first electrode and the second electrode are made of a graphite material or a metal.

在一實施例中,更包括一進液單元以及一排氣單元。 In an embodiment, a liquid inlet unit and an exhaust unit are further included.

承上所述,本發明可透過於第一電極與第二電極之間夾置多 孔填充材,且透過多孔填充材使得電解液得以均勻地與電極上的石墨烯材料反應。因此,本發明得可實現提供一種能於常溫下生產,成本低廉、提升效率及提高整體生產高品質的石墨烯生成裝置的目的。 According to the above, the present invention can be interposed between the first electrode and the second electrode. The pore filler and the porous filler material allow the electrolyte to react uniformly with the graphene material on the electrode. Therefore, the present invention can achieve the object of providing a graphene generating device which can be produced at normal temperature, has low cost, improves efficiency, and improves overall production quality.

1‧‧‧石墨烯生成裝置 1‧‧‧graphene generating device

10、10a‧‧‧電解槽 10, 10a‧‧‧ Electrolyzer

11、11a‧‧‧第一電極 11, 11a‧‧‧ first electrode

12、12a‧‧‧第二電極 12, 12a‧‧‧ second electrode

13、13a‧‧‧石墨烯材料 13, 13a‧‧‧Graphene materials

14、14a‧‧‧多孔填充材 14, 14a‧‧‧ Porous filler

15‧‧‧電源供應器 15‧‧‧Power supply

16、16a‧‧‧進液單元 16, 16a‧‧‧ Inlet unit

17a‧‧‧濾網 17a‧‧‧Filter

18、18a‧‧‧夾具 18, 18a‧‧‧ fixture

S‧‧‧電解液 S‧‧‧ electrolyte

圖1為一種本發明的石墨烯生成裝置的第一實施例的立體示意圖。 BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a perspective view showing a first embodiment of a graphene producing apparatus of the present invention.

圖2為圖1的實施例的側面示意圖。 Figure 2 is a side elevational view of the embodiment of Figure 1.

圖3為透過本發明的石墨烯生成裝置與習知電化學剝離製程的又一數量比例-產量長條圖。 Figure 3 is a further graph of the production-through bar graph of the graphene generating apparatus of the present invention and a conventional electrochemical stripping process.

圖4為透過本發明的石墨烯生成裝置與習知電化學剝離製程的厚度分布-比例長條圖。 4 is a thickness distribution-proportional bar graph of a graphene generating apparatus and a conventional electrochemical stripping process of the present invention.

圖5為一種本發明的石墨烯生成裝置的第二實施例的側面示意圖。 Figure 5 is a side elevational view of a second embodiment of a graphene generating apparatus of the present invention.

以下將參照相關圖式,說明依本發明較佳實施例之一種石墨烯生成裝置,其中相同的元件將以相同的參照符號加以說明。 DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a graphene generating apparatus according to a preferred embodiment of the present invention will be described with reference to the accompanying drawings, wherein the same elements will be described with the same reference numerals.

請先參考圖1至圖4,圖1為一種本發明的石墨烯生成裝置的第一實施例的立體示意圖。圖2為圖1的實施例的側面示意圖。圖3為透過本發明的石墨烯生成裝置與習知電化學剝離製程的產率-長條圖。圖4為透過本發明的石墨烯生成裝置與習知電化學剝離製程的厚度分布-比例長條圖。 Please refer to FIG. 1 to FIG. 4, which is a perspective view of a first embodiment of a graphene generating device of the present invention. Figure 2 is a side elevational view of the embodiment of Figure 1. Fig. 3 is a graph showing the yield-bar graph of the graphene generating apparatus of the present invention and a conventional electrochemical stripping process. 4 is a thickness distribution-proportional bar graph of a graphene generating apparatus and a conventional electrochemical stripping process of the present invention.

本發明的第一實施例的石墨烯生成裝置1,包括電解槽10、至少一第一電極11、至少一第二電極12、石墨烯材料13、多孔填充材14以及夾具18。 The graphene generating apparatus 1 of the first embodiment of the present invention includes an electrolytic cell 10, at least a first electrode 11, at least a second electrode 12, a graphene material 13, a porous filler 14, and a jig 18.

本實施例的電解槽10具有一容置槽體,得以填充電解液S。本實施例的電解液S可為石墨烯溶液。 The electrolytic cell 10 of the present embodiment has a housing tank to fill the electrolyte S. The electrolytic solution S of the present embodiment may be a graphene solution.

請特別參考圖1以及圖2,至少一第二電極12與第一電極11會相對設置,且第一電極11與第二電極12可形成一電極模組。此外,且本實施例的第一電極11為一惰性電極,為石墨材料或金屬所製成。本實 施例的第二電極12亦可為石墨材料或金屬所製成,此處的石墨材料或是金屬材料例如可為天然石墨、人造石墨、銅、不銹鋼、白金等材料所製成,但不以此些材料為限制。 Referring to FIG. 1 and FIG. 2 , at least one second electrode 12 and the first electrode 11 are disposed opposite to each other, and the first electrode 11 and the second electrode 12 can form an electrode module. In addition, the first electrode 11 of the embodiment is an inert electrode made of a graphite material or a metal. Real The second electrode 12 of the embodiment may also be made of a graphite material or a metal. The graphite material or the metal material herein may be made of natural graphite, artificial graphite, copper, stainless steel, platinum, etc., but not These materials are limited.

此外,本實施例的石墨烯材料13可設置於第二電極12。且此處的石墨烯材料13的設置方式可為部份或是全數覆蓋第二電極12的方式為之。此處的石墨烯材料13可選用天然石墨、人造石墨等任何具石墨化排列之碳材料皆可。 Further, the graphene material 13 of the present embodiment may be disposed on the second electrode 12. The manner in which the graphene material 13 is disposed may be partially or completely covered by the second electrode 12. Here, the graphene material 13 may be any carbon material having a graphitized arrangement such as natural graphite or artificial graphite.

多孔填充材14可設置於第一電極11以及第二電極12之間。詳而言之,多孔填充材14更可設置於石墨烯材料13以及第二電極12之間,故,透過此配置,本實施例設置的多孔填充材14可避免第二電極12與石墨烯材料13接觸造成短路的問題。且亦可透過不同的多孔填充材14調整第一電極11以及第二電極12的距離(間隔距離即為多孔填充材14的厚度)進而調整整體的反應速度。簡言之,透過本實施例此種配置,可更有效的堆疊複數個電極模組於電解槽10,並可有效的提高整體的產量。 The porous filler 14 may be disposed between the first electrode 11 and the second electrode 12. In detail, the porous filler 14 can be disposed between the graphene material 13 and the second electrode 12, so that the porous filler 14 provided in the embodiment can avoid the second electrode 12 and the graphene material. 13 contact caused a short circuit problem. Further, the distance between the first electrode 11 and the second electrode 12 (the separation distance is the thickness of the porous filler 14) can be adjusted by different porous fillers 14 to adjust the overall reaction rate. In short, with this configuration of the embodiment, a plurality of electrode modules can be stacked more efficiently in the electrolytic cell 10, and the overall yield can be effectively improved.

此外,更利用其上的孔洞使電解液S均勻的被引導至第一電極11以及第二電極12的表面,並產生電化學反應。最後再透過其上的孔洞將電化學反應中產生的氣體排出。補充說明的是,透過多孔填充材14的孔洞,石墨烯材料13的表面得以均勻的與電解液S產生反應,並可控制其反應的深度約為1mm~30mm之間,較佳地可限制1mm~10mm之間,故剝落的石墨烯產物厚度得以被控制。 Further, the pores on the electrolyte solution S are uniformly guided to the surfaces of the first electrode 11 and the second electrode 12, and an electrochemical reaction is generated. Finally, the gas generated in the electrochemical reaction is discharged through the holes in the hole. It is added that the surface of the graphene material 13 is uniformly reacted with the electrolyte S through the pores of the porous filler material 14, and the depth of the reaction can be controlled to be between about 1 mm and 30 mm, preferably 1 mm. Between ~10mm, the thickness of the exfoliated graphene product can be controlled.

且,本實施例的多孔填充材14可選用多孔陶瓷板、海綿、發泡塑膠、塑膠網、沸石、石英綿或其組合,但不以此些材料為限制。且本實施例可選用、搭配的多孔填充材14的孔徑大小可介於5μm至1mm之間。 Moreover, the porous filler material 14 of the present embodiment may be a porous ceramic plate, a sponge, a foamed plastic, a plastic mesh, a zeolite, a quartz wool or a combination thereof, but is not limited by these materials. Moreover, the porous filler material 14 that can be used and matched in this embodiment can have a pore size of between 5 μm and 1 mm.

夾具18得以夾置第一電極11與第二電極12,換言之,本實施例的第一電極11與第二電極12是以固定、設置於夾具18之間。故透過夾具18的設置,本實施例的石墨烯材料13可被固定、侷限於多孔材料14與第二電極12之間,因而使得石墨烯材料13得以完全反應,且可達到80%的剝離程度。 The jig 18 is capable of sandwiching the first electrode 11 and the second electrode 12, in other words, the first electrode 11 and the second electrode 12 of the present embodiment are fixed and disposed between the jigs 18. Therefore, through the arrangement of the jig 18, the graphene material 13 of the present embodiment can be fixed and limited between the porous material 14 and the second electrode 12, thereby allowing the graphene material 13 to be completely reacted and achieving a peeling degree of 80%. .

此外,本實施例的石墨烯生成裝置1更可包括電源供應器15,分別與第一電極11與第二電極12電性連接,並使第一電極11與第二電極12產生一電勢差。且電源供應器15可提供直流電或交流電。 In addition, the graphene generating device 1 of the present embodiment may further include a power supply 15 electrically connected to the first electrode 11 and the second electrode 12, respectively, and generating a potential difference between the first electrode 11 and the second electrode 12. And the power supply 15 can provide direct current or alternating current.

另外,本實施例的石墨烯生成裝置1更可包括更包括進液單元16以及排氣單元(圖未示出)。進液單元16用以補充電解液S,而排氣單元則用以將反應中產生之氣體的排出。 In addition, the graphene generating device 1 of the present embodiment may further include a liquid inlet unit 16 and an exhaust unit (not shown). The liquid inlet unit 16 is used to replenish the electrolyte S, and the exhaust unit is used to discharge the gas generated in the reaction.

實際操作時,依序將第一電極11、第二電極12及多孔填充材14安裝於電解槽10中。接著,電解液S透過多孔填充材14的孔洞引導使電解液S與第二電極12上的石墨烯材料13接觸。 In actual operation, the first electrode 11, the second electrode 12, and the porous filler 14 are sequentially mounted in the electrolytic cell 10. Next, the electrolyte S is guided through the pores of the porous filler 14 to bring the electrolyte S into contact with the graphene material 13 on the second electrode 12.

第一電極11與第二電極12具有電勢差,在反應過程中,電勢差將會使得電解液S電解並產生氫氣與氧氣,此些氣體可透過多孔介質上溢散。且本實施例的電勢差可介於5伏特至100伏特之間。較佳地,電勢差更可介於10伏特至50伏特之間。 The first electrode 11 and the second electrode 12 have a potential difference. During the reaction, the potential difference causes the electrolyte S to electrolyze and generate hydrogen and oxygen, which are permeable to the porous medium. And the potential difference of this embodiment may be between 5 volts and 100 volts. Preferably, the potential difference can be between 10 volts and 50 volts.

產生氣體的同時,將會造成第一電極11表面的石墨單層或是多層膨脹,並剝離成為石墨烯薄片或石墨烯粉末。而剝離的石墨烯將留在電解槽10中。最後再將剝離的石墨烯真空乾燥得到產物。 At the same time as the gas is generated, the graphite single layer or the plurality of layers on the surface of the first electrode 11 is expanded and peeled off into a graphene sheet or a graphene powder. The stripped graphene will remain in the electrolytic cell 10. Finally, the stripped graphene is vacuum dried to obtain a product.

以下將例示本實施例可能搭配的方式。 The manner in which this embodiment may be matched will be exemplified below.

舉例而言,本實施例的石墨烯材料可為石墨粉,搭配氧化鋁的多孔填充材14。氧化鋁的平均孔徑可為5μm,且本實施例的多孔填充材14的厚度為5mm,換言之,本實施例的第一電極11與第二電極12的間距即為5mm。電解液為溶於300ml的0.25M硫酸(操作溫度可介於室溫至40℃)。施加電勢差為10V,電流約為2A,在反應時間為8小時下,約可生成50mg的石墨烯粉末。 For example, the graphene material of the present embodiment may be a graphite powder, with a porous filler material 14 of alumina. The average pore diameter of the alumina may be 5 μm, and the thickness of the porous filler 14 of the present embodiment is 5 mm. In other words, the pitch of the first electrode 11 and the second electrode 12 of the present embodiment is 5 mm. The electrolyte was dissolved in 300 ml of 0.25 M sulfuric acid (operating temperature may range from room temperature to 40 ° C). The applied potential difference was 10 V, the current was about 2 A, and about 50 mg of graphene powder was produced at a reaction time of 8 hours.

補充說明的是,本實施例的多孔填充材14的孔徑將會依據電解液S補充的速度、氣體逸散的速度作為選用的依據。此外亦可通過調整電解液S的濃度、電解質的種類、溶劑類型以及電勢差來改變石墨烯的剝離速度、性質以及產量。 It should be noted that the pore diameter of the porous filler material 14 of the present embodiment will be selected according to the speed of the electrolyte solution S and the speed of gas escape. In addition, the peeling speed, properties, and yield of graphene can be changed by adjusting the concentration of the electrolyte S, the type of the electrolyte, the type of the solvent, and the potential difference.

且,本實施例的石墨烯生成裝置1於其他的實施態樣中,亦可包括過濾與分離產物模組。為了實現連續化製程的目的,本實施例的石 墨烯生成裝置1所剝離的產物可透過過濾與分離產物之模組的微孔隙之篩網過濾未剝離之粗粒徑石墨顆粒,以及透過篩選得到適當尺寸之產物後(一般為10nm以下的薄層石墨烯),再以大量去離子水來去除殘留之電解液,或以其他可以溶解、取代殘餘離子之離子溶液。 Moreover, in other embodiments, the graphene generating device 1 of the present embodiment may further include a filtering and separating product module. The stone of the present embodiment for the purpose of achieving a continuous process The product stripped by the olefin generating device 1 can be passed through a microporous screen of a module for filtering and separating products to filter unpeeled coarse-grained graphite particles, and after screening to obtain a product of an appropriate size (generally thinner than 10 nm) Layer graphene), and then a large amount of deionized water to remove residual electrolyte, or other ionic solution that can dissolve and replace residual ions.

請接著參考圖3以及圖4,圖3為透過本發明的石墨烯生成裝置與習知電化學剝離製程的產率-長條圖。圖4為透過本發明的石墨烯生成裝置與習知電化學剝離製程的厚度分布-比例長條圖。圖4為圖3中500目數以下的石墨烯的厚度分佈示意圖。 Referring to FIG. 3 and FIG. 4, FIG. 3 is a yield-bar graph of the graphene generating apparatus of the present invention and a conventional electrochemical stripping process. 4 is a thickness distribution-proportional bar graph of a graphene generating apparatus and a conventional electrochemical stripping process of the present invention. 4 is a schematic view showing the thickness distribution of graphene of 500 mesh or less in FIG.

且圖面中繪製的圖表僅為本發明的其一實施例示意,其多孔填充材為多孔陶瓷板,並可搭配0.25M的硫酸作為其電解液。但可能會依據不同的多孔填充材以及電解液使得數據有所微調,但其各實施例間的整體的效果相似。 The graph drawn in the drawing is only an embodiment of the present invention, and the porous filler is a porous ceramic plate and can be combined with 0.25 M sulfuric acid as its electrolyte. However, the data may be fine-tuned according to different porous filler materials and electrolytes, but the overall effect between the various embodiments is similar.

因,習知電化學剝離的主要的產量的峰值大多落在500目數以上(mesh),且生成的厚度的峰值為10~20nm。本發明的石墨烯生成裝置,石墨烯的主要產量的峰值將會落在500目數(mesh)以下,且生成的厚度多數落在5~10nm的區間。而5~10nm的石墨烯產物實為實際上應用且被篩選出作用後續加工的區間。換言之,透過本發明的石墨烯生成裝置可將產物中可用的石墨烯的產量大幅提昇,以達到提升效率及提高整體生產高品質的目的。 For example, the peak of the main yield of the conventional electrochemical stripping mostly falls below 500 mesh, and the peak of the generated thickness is 10-20 nm. In the graphene generating apparatus of the present invention, the peak value of the main yield of graphene will fall below 500 mesh, and the generated thickness mostly falls within the range of 5 to 10 nm. The 5-10 nm graphene product is actually applied and screened out for the subsequent processing. In other words, the graphene production device of the present invention can greatly increase the yield of graphene available in the product, thereby achieving the purpose of improving efficiency and improving overall production quality.

且,本發明的石墨烯生成裝置與習知電化學剝離製程相比,至少具有以下優點,一者本發明所採用的電壓較低、操作溫度為常溫、產物的厚度將會集中於業界所需的標準、裝置結構簡單、操作容易,因此本發明將能應用於並符合大量生產的需求。 Moreover, the graphene generating device of the present invention has at least the following advantages compared with the conventional electrochemical stripping process. One of the voltages used in the present invention is low, the operating temperature is normal temperature, and the thickness of the product is concentrated in the industry. The standard, the device structure is simple, and the operation is easy, so the present invention can be applied to and meet the requirements of mass production.

最後,請參考圖5,其為一種本發明的石墨烯生成裝置的第二實施例的側面示意圖。 Finally, please refer to FIG. 5, which is a side view of a second embodiment of the graphene generating device of the present invention.

相似地,本實施例的石墨烯生成裝置1a,包括電解槽10a、至少一第一電極11a、至少一第二電極12a、石墨烯材料13a、多孔填充材14a以及夾具18a。且本實施例亦包括一進液單元16a。 Similarly, the graphene generating apparatus 1a of the present embodiment includes an electrolytic cell 10a, at least one first electrode 11a, at least one second electrode 12a, a graphene material 13a, a porous filler 14a, and a jig 18a. And this embodiment also includes a liquid inlet unit 16a.

與前述實施例相異處有二,一者本實施例的石墨烯生成裝置 1a的具有兩組電極,且各組電極包括第一電極11a以及一第二電極12a。換言之,本發明的第一電極11a及第二電極12a並不侷限於一組,也模組化以並聯的方式合併多組。 Different from the foregoing embodiment, there is two, one of the graphene generating devices of the present embodiment 1a has two sets of electrodes, and each set of electrodes includes a first electrode 11a and a second electrode 12a. In other words, the first electrode 11a and the second electrode 12a of the present invention are not limited to one set, and are modularized to combine a plurality of groups in parallel.

此外,本實施例的石墨烯生成裝置更包括濾網17a,設置於多孔填充材14a與石墨烯材料13a之間。於第一電極11a上設置濾網17a的目的在於可避免第一電極11a未反應完全的石墨進入多孔填充材14a,使得多孔填充材14a的孔洞將不會被堵塞。且可透過濾網17a加強電解液的擴散程度。 Further, the graphene producing apparatus of the present embodiment further includes a screen 17a disposed between the porous filler 14a and the graphene material 13a. The purpose of providing the screen 17a on the first electrode 11a is to prevent the unreacted graphite of the first electrode 11a from entering the porous filler 14a, so that the pores of the porous filler 14a will not be clogged. And the filter 17a can be permeable to enhance the degree of diffusion of the electrolyte.

此外,本實施例的濾網17a更可設置於第二電極12a與多孔填充材14a之間,此處設置濾網17a的目的在於避免第二電極12a上的石墨烯材料13a進入多孔填充材14a。簡言之,可透過在多孔填充材14a的表面配置濾網17a,以提高本裝置的整體效率。 In addition, the screen 17a of the present embodiment may be disposed between the second electrode 12a and the porous filler 14a. The purpose of the screen 17a is to prevent the graphene material 13a on the second electrode 12a from entering the porous filler 14a. . In short, the filter 17a can be disposed on the surface of the porous filler 14a to improve the overall efficiency of the apparatus.

舉例而言,本實施例的石墨烯材料13a可石墨粉,多孔填充材14a則為海綿,其平均孔徑約為1mm,其厚度為10mm(本實施例的第一電極11a與第二電極12a的間距即為10mm)。濾網17a可為尼龍網(其網目大小約為300um),透過對第一電極11a以及第二電極12a施加電壓20V,電流約為10A,總反應時間為8小時,電解液為溶於300ml的0.25M硫酸溶液搭配30ml的氫氧化鉀(30wt%),且操作溫度可介於室溫至40℃。在此種配置下,石墨烯的產量約為500mg。 For example, the graphene material 13a of the present embodiment may be graphite powder, and the porous filler material 14a is a sponge having an average pore diameter of about 1 mm and a thickness of 10 mm (the first electrode 11a and the second electrode 12a of the present embodiment). The pitch is 10mm). The strainer 17a may be a nylon mesh (having a mesh size of about 300 um), and a voltage of 20 V is applied to the first electrode 11a and the second electrode 12a, the current is about 10 A, the total reaction time is 8 hours, and the electrolyte is dissolved in 300 ml. The 0.25 M sulfuric acid solution was combined with 30 ml of potassium hydroxide (30 wt%) and the operating temperature was between room temperature and 40 °C. In this configuration, the yield of graphene is about 500 mg.

綜上所述,透過於第一電極與第二電極之間夾置多孔填充材、透過夾具將石墨烯材料固定於第二電極與多孔填充材之間,再搭配多孔填充材使得電解液得以均勻地與電極上的石墨烯材料反應。因此,本發明得可實現提供一種能於常溫下生產,成本低廉、提升效率、提高整體生產高品質、減少電極短路的石墨烯生成裝置的目的。 In summary, the porous filler material is interposed between the first electrode and the second electrode, and the graphene material is fixed between the second electrode and the porous filler through the jig, and then the porous filler is used to make the electrolyte uniform. The ground reacts with the graphene material on the electrode. Therefore, the present invention can achieve the object of providing a graphene generating device which can be produced at normal temperature, has low cost, improves efficiency, improves overall production quality, and reduces electrode short circuit.

以上所述僅為舉例性,而非為限制性者。任何未脫離本發明之精神與範疇,而對其進行之等效修改或變更,均應包含於後附之申請專利範圍中。 The above is intended to be illustrative only and not limiting. Any equivalent modifications or alterations to the spirit and scope of the invention are intended to be included in the scope of the appended claims.

1‧‧‧石墨烯生成裝置 1‧‧‧graphene generating device

10‧‧‧電解槽 10‧‧‧electrolyzer

11‧‧‧第一電極 11‧‧‧First electrode

12‧‧‧第二電極 12‧‧‧Second electrode

13‧‧‧石墨烯材料 13‧‧‧Graphene materials

14‧‧‧多孔填充材 14‧‧‧Porous filler

16‧‧‧進液單元 16‧‧‧Inlet unit

18‧‧‧夾具 18‧‧‧Clamp

S‧‧‧電解液 S‧‧‧ electrolyte

Claims (9)

一種石墨烯生成裝置,包括:一電解槽,填充一電解液;一夾具;至少一第一電極;至少一第二電極,與該第一電極相對設置,且該夾具夾置該第一電極與該第二電極;一石墨烯材料,設置於該第二電極;以及一多孔填充材,設置於該第一電極以及該第二電極之間。 A graphene generating device comprising: an electrolytic cell filled with an electrolyte; a clamp; at least one first electrode; at least one second electrode disposed opposite to the first electrode, and the clamp sandwiches the first electrode The second electrode; a graphene material disposed on the second electrode; and a porous filler disposed between the first electrode and the second electrode. 如申請專利範圍第1項所述的裝置,更包括一電源供應器,分別與該第一電極與該第二電極電性連接,並使該第一電極與該第二電極產生一電勢差。 The device of claim 1, further comprising a power supply electrically connected to the first electrode and the second electrode, respectively, and causing a potential difference between the first electrode and the second electrode. 如申請專利範圍第2項所述的裝置,其中該第一電極與該第二電極具有一電勢差,且該電勢差介於5伏特至100伏特之間。 The device of claim 2, wherein the first electrode and the second electrode have a potential difference, and the potential difference is between 5 volts and 100 volts. 如申請專利範圍第3項所述的裝置,其中該電勢差介於10伏特至50伏特之間。 The device of claim 3, wherein the potential difference is between 10 volts and 50 volts. 如申請專利範圍第1項所述的裝置,更包括一濾網,設置於該多孔填充材與該石墨烯材料之間。 The device of claim 1, further comprising a screen disposed between the porous filler and the graphene material. 如申請專利範圍第1項所述的裝置,其中該多孔填充材的孔徑大小介於5μm至1mm之間。 The device of claim 1, wherein the porous filler has a pore size between 5 μm and 1 mm. 如申請專利範圍第1項所述的裝置,其中該多孔填充材為多孔陶瓷板、海綿、發泡塑膠、塑膠網、沸石、石英綿或其組合。 The device of claim 1, wherein the porous filler material is a porous ceramic plate, a sponge, a foamed plastic, a plastic mesh, a zeolite, a quartz wool, or a combination thereof. 如申請專利範圍第1項所述的裝置,其中該第一電極及該第二電極為石墨材料或金屬所製成。 The device of claim 1, wherein the first electrode and the second electrode are made of a graphite material or a metal. 如申請專利範圍第1項所述的裝置,更包括一進液單元以及一排氣單元。 The device of claim 1, further comprising a liquid inlet unit and an exhaust unit.
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