TWI842351B - Method for producing silver nanoparticles - Google Patents

Method for producing silver nanoparticles Download PDF

Info

Publication number
TWI842351B
TWI842351B TW112102482A TW112102482A TWI842351B TW I842351 B TWI842351 B TW I842351B TW 112102482 A TW112102482 A TW 112102482A TW 112102482 A TW112102482 A TW 112102482A TW I842351 B TWI842351 B TW I842351B
Authority
TW
Taiwan
Prior art keywords
silver
particle size
crystal growth
silver nanoparticles
electrode
Prior art date
Application number
TW112102482A
Other languages
Chinese (zh)
Other versions
TW202430722A (en
Inventor
李佳任
林建宏
蕭博文
Original Assignee
國立高雄師範大學
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 國立高雄師範大學 filed Critical 國立高雄師範大學
Priority to TW112102482A priority Critical patent/TWI842351B/en
Application granted granted Critical
Publication of TWI842351B publication Critical patent/TWI842351B/en
Publication of TW202430722A publication Critical patent/TW202430722A/en

Links

Images

Landscapes

  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

The present invention relates to a method for producing silver nanoparticles. Silver nuclei are produced by an electrochemical reaction in an electrolyte with a high concentration of a size-controlling agent in the method for producing the silver nanoparticles. Then, a portion of the size-controlling agent is removed from the electrolyte, such that the silver nuclei grow in a crystal growth solution with a low concentration of the size-controlling agent. As a crystallizing time is increased, an initial particle size of the silver nuclei is increased, so as to form the silver nanoparticles. At a specific crystallizing time, a portion taken from the crystal growth solution can obtain the silver nanoparticles with a specific average particle size, thereby simplifying the process and saving time.

Description

銀奈米粒子的製造方法Method for producing silver nanoparticles

本發明係有關於一種銀奈米粒子的製造方法,且特別是有關於一種從同一個長晶溶液獲得不同平均粒徑之銀奈米粒子的製造方法。 The present invention relates to a method for producing silver nanoparticles, and in particular to a method for producing silver nanoparticles with different average particle sizes from the same crystal growth solution.

在習知之銀奈米粒子的製造方法中,製程包括施加電流於單一種電解液中,以透過電化學反應生成複數個銀核子。然後,停止施加電流後,經過一段固定的長晶時間,此些銀核子長晶成具有一種特定平均粒徑之銀奈米粒子。 In the known method of manufacturing silver nanoparticles, the process includes applying a current to a single electrolyte to generate a plurality of silver nuclei through an electrochemical reaction. Then, after stopping the application of the current, after a fixed growth time, these silver nuclei grow into silver nanoparticles with a specific average particle size.

如上所述,習知銀奈米粒子的製程僅能由單一種電解液製得具備一種特定平均粒徑之銀奈米粒子。若想要獲得多種平均粒徑之銀奈米粒子,需要進行多個製程。再者,習知銀奈米粒子的製程尚需要使用不同的試劑及不同的製程條件,以製得對應之平均粒徑的銀奈米粒子,故大幅增加製造成本且浪費時間。有鑑於此,亟需發展一種新的銀奈米粒子之製造方法,以改善上述缺點。 As mentioned above, the conventional process of making silver nanoparticles can only produce silver nanoparticles with a specific average particle size from a single electrolyte. If you want to obtain silver nanoparticles with multiple average particle sizes, you need to perform multiple processes. Furthermore, the conventional process of making silver nanoparticles still requires the use of different reagents and different process conditions to obtain silver nanoparticles with corresponding average particle sizes, which greatly increases the manufacturing cost and wastes time. In view of this, it is urgent to develop a new method for making silver nanoparticles to improve the above shortcomings.

有鑑於上述之問題,本發明之一態樣是在提供一種銀奈米粒子的製造方法。於此製造方法中,從同一長晶溶液於特定長晶時間取出之一部分,可獲得具有特定平均粒徑之銀奈米粒子,從而簡化製程並節省時間。 In view of the above problems, one aspect of the present invention is to provide a method for manufacturing silver nanoparticles. In this manufacturing method, a portion of the same crystal growth solution is taken out at a specific crystal growth time to obtain silver nanoparticles with a specific average particle size, thereby simplifying the process and saving time.

根據本發明之一態樣,提出一種銀奈米粒子的製造方法。於銀奈米粒子的製造方法中,先提供電化學反應系統,其中電化學反應系統包含做為正極之銀電極、做為負極之相對電極、電解液及電力供應元件。電解液接觸銀電極的一端及相對電極的一端,且電解液包含粒徑控制試劑,此粒徑控制試劑之濃度為0.08M至0.12M。電力供應元件分別電性連接銀電極的另一端及相對電極的另一端。然後,對電化學反應系統進行電化學反應,其中施加定電流至銀電極及相對電極,以電解銀電極成為複數個銀離子,且此些銀離子從相對電極接收電子後,生成複數個銀核子。接續,停止施加定電流,並去除電解液中粒徑控制試劑之一部分,直至濃度降低到3x10-8M至5x10-8M,以獲得長晶溶液。之後,對此些銀核子進行長晶步驟,以獲得此些銀奈米粒子,其中此些銀核子之初始粒徑隨著長晶時間增大,且於不同的長晶時間取出電解液之一部分,以獲得具有特定的平均粒徑之此些銀奈米粒子,且平均粒徑之分佈範圍為25奈米至150奈米。 According to one aspect of the present invention, a method for manufacturing silver nanoparticles is provided. In the method for manufacturing silver nanoparticles, an electrochemical reaction system is first provided, wherein the electrochemical reaction system includes a silver electrode as a positive electrode, an opposite electrode as a negative electrode, an electrolyte, and a power supply element. The electrolyte contacts one end of the silver electrode and one end of the opposite electrode, and the electrolyte includes a particle size control reagent, and the concentration of the particle size control reagent is 0.08M to 0.12M. The power supply element is electrically connected to the other end of the silver electrode and the other end of the opposite electrode, respectively. Then, an electrochemical reaction is performed on the electrochemical reaction system, wherein a constant current is applied to the silver electrode and the counter electrode to electrolyze the silver electrode into a plurality of silver ions, and these silver ions generate a plurality of silver nuclei after receiving electrons from the counter electrode. Subsequently, the application of the constant current is stopped, and a portion of the particle size control reagent in the electrolyte is removed until the concentration is reduced to 3x10-8 M to 5x10-8 M, so as to obtain a crystal growth solution. Afterwards, a crystal growth step is performed on these silver nuclei to obtain these silver nanoparticles, wherein the initial particle size of these silver nuclei increases with the crystal growth time, and a portion of the electrolyte is taken out at different crystal growth times to obtain these silver nanoparticles with a specific average particle size, and the distribution range of the average particle size is 25 nanometers to 150 nanometers.

依據本發明之一實施例,電解液更包含丙酮。 According to one embodiment of the present invention, the electrolyte further comprises acetone.

依據本發明之另一實施例,粒徑控制試劑包含十二 烷基硫酸鈉。 According to another embodiment of the present invention, the particle size control reagent comprises sodium dodecyl sulfate.

依據本發明之又一實施例,定電流為90毫安培至110毫安培。 According to another embodiment of the present invention, the set current is 90 mA to 110 mA.

依據本發明之又一實施例,電化學反應之反應時間為20秒至1分鐘。 According to another embodiment of the present invention, the reaction time of the electrochemical reaction is 20 seconds to 1 minute.

依據本發明之又一實施例,電化學反應之反應溫度為28℃至32℃。 According to another embodiment of the present invention, the reaction temperature of the electrochemical reaction is 28°C to 32°C.

依據本發明之又一實施例,在電化學反應期間,擾動電解液。 According to another embodiment of the present invention, the electrolyte is disturbed during the electrochemical reaction.

依據本發明之又一實施例,於電化學反應中,此些銀核子生成於粒徑控制試劑所形成之複數個微胞內部。 According to another embodiment of the present invention, in an electrochemical reaction, these silver nuclei are generated inside a plurality of micelles formed by a particle size control reagent.

依據本發明之又一實施例,於長晶步驟中,初始粒徑係依據以下方程式(1)而增大。 According to another embodiment of the present invention, in the crystal growth step, the initial grain size increases according to the following equation (1).

d=a+b×t (1) d = a + b × t (1)

於方程式(1)中,a代表常數,d代表初始粒徑(奈米),t代表長晶時間(小時),並且當長晶時間短於8.3小時的時候,a為27至28,b為10至10.5(奈米/小時),或者當長晶時間為8.3小時至98.5小時之間,a為106至107,b為0.4至0.45(奈米/小時)。 In equation (1), a represents a constant, d represents the initial particle size (nanometers), t represents the crystal growth time (hours), and when the crystal growth time is shorter than 8.3 hours, a is 27 to 28 and b is 10 to 10.5 (nanometers/hour), or when the crystal growth time is between 8.3 hours and 98.5 hours, a is 106 to 107 and b is 0.4 to 0.45 (nanometers/hour).

依據本發明之又一實施例,於長晶步驟後,銀奈米粒子的製造方法更包含終止步驟,藉由提高此些溶液中之粒徑控制試劑之濃度至大於0.15M,以停止長晶步驟。 According to another embodiment of the present invention, after the crystal growth step, the method for manufacturing silver nanoparticles further includes a termination step, by increasing the concentration of the particle size control reagent in these solutions to greater than 0.15M to stop the crystal growth step.

應用本發明之銀奈米粒子的製造方法,其中於包含高濃度的粒徑控制試劑之電解液下,利用電化學反應生成 銀核子。然後,從電解液中移除粒徑控制試劑之一部分,以使銀核子於包含低濃度的粒徑控制試劑之長晶溶液中長晶成銀奈米粒子。從同一個長晶溶液於特定長晶時間取出之一部分可獲得具有特定平均粒徑之銀奈米粒子,從而簡化製程並節省時間。 The manufacturing method of silver nanoparticles of the present invention is applied, wherein silver nuclei are generated by electrochemical reaction in an electrolyte containing a high concentration of a particle size control reagent. Then, a portion of the particle size control reagent is removed from the electrolyte so that the silver nuclei grow into silver nanoparticles in a crystal growth solution containing a low concentration of a particle size control reagent. Silver nanoparticles with a specific average particle size can be obtained by taking out a portion from the same crystal growth solution at a specific crystal growth time, thereby simplifying the process and saving time.

100:方法 100:Methods

110,120,130,140:操作 110,120,130,140: Operation

為了對本發明之實施例及其優點有更完整之理解,現請參照以下之說明並配合相應之圖式。必須強調的是,各種特徵並非依比例描繪且僅係為了圖解目的。相關圖式內容說明如下:圖1係繪示根據本發明之一實施例之銀奈米粒子的製造方法之流程圖。 In order to have a more complete understanding of the embodiments of the present invention and its advantages, please refer to the following description and the corresponding drawings. It must be emphasized that the various features are not drawn to scale and are only for illustration purposes. The contents of the relevant drawings are described as follows: Figure 1 is a flow chart of a method for manufacturing silver nanoparticles according to an embodiment of the present invention.

圖2係繪示本發明之實施例1、比較例1及比較例2之銀核子的初始粒徑隨著長晶時間的增加而增大的情形。 Figure 2 shows how the initial grain size of the silver nuclei of Example 1, Comparative Example 1 and Comparative Example 2 of the present invention increases with the increase of crystal growth time.

以下仔細討論本發明實施例之製造和使用。然而,可以理解的是,實施例提供許多可應用的發明概念,其可實施於各式各樣的特定內容中。所討論之特定實施例僅供說明,並非用以限定本發明之範圍。 The manufacture and use of embodiments of the present invention are discussed in detail below. However, it is understood that the embodiments provide many applicable inventive concepts that can be implemented in a variety of specific contexts. The specific embodiments discussed are for illustration only and are not intended to limit the scope of the present invention.

請參閱圖1,於銀奈米粒子的製造方法100中,提供電化學反應系統,如操作110所示。電化學反應系統包含銀電極、相對電極、電解液及電力供應元件。前述之 銀電極及相對電極分別做為正極及負極。相對電極可為導電的材料,其具體例可包含但不限於白金、石墨或其他金屬材料。 Please refer to FIG. 1 . In the method 100 for manufacturing silver nanoparticles, an electrochemical reaction system is provided, as shown in operation 110. The electrochemical reaction system includes a silver electrode, a counter electrode, an electrolyte, and a power supply element. The aforementioned silver electrode and the counter electrode serve as a positive electrode and a negative electrode, respectively. The counter electrode may be a conductive material, and its specific examples may include but are not limited to platinum, graphite, or other metal materials.

電解液接觸銀電極的一端及相對電極的一端,並且電力供應元件分別電性連接銀電極的另一端及相對電極的另一端。詳述之,電解液包含粒徑控制試劑,例如十二烷基硫酸鈉。在一些具體例中,粒徑控制試劑之濃度為0.08M至0.12M,且較佳可為0.09M至0.11M。倘若,粒徑控制試劑之濃度低於0.08M,粒徑控制試劑難以形成微胞,故於後述之電化學反應中生成之銀核子容易聚集,而不能控制製得之銀奈米粒子的平均粒徑。反之,倘若粒徑控制試劑之濃度高於0.12M,導致粒徑控制試劑所形成之微胞中的多數者內部沒有後述之電解銀電極所產生之銀離子,故未能生成銀核子,或者於後續去除電解液中部份的粒徑控制試劑之步驟中需要進行多次去除,此可能移除電解液中的銀原子及/或銀核子,而影響後續長晶步驟,故使製得之銀奈米粒子的平均粒徑不在預期範圍內。 The electrolyte contacts one end of the silver electrode and one end of the opposite electrode, and the power supply element is electrically connected to the other end of the silver electrode and the other end of the opposite electrode, respectively. In detail, the electrolyte contains a particle size control reagent, such as sodium dodecyl sulfate. In some specific examples, the concentration of the particle size control reagent is 0.08M to 0.12M, and preferably 0.09M to 0.11M. If the concentration of the particle size control reagent is lower than 0.08M, the particle size control reagent is difficult to form micelles, so the silver nuclei generated in the electrochemical reaction described later are easy to aggregate, and the average particle size of the obtained silver nanoparticles cannot be controlled. On the contrary, if the concentration of the particle size control reagent is higher than 0.12M, most of the micelles formed by the particle size control reagent will not contain the silver ions generated by the electrolytic silver electrode described later, so silver nuclei cannot be generated, or the particle size control reagent in the subsequent removal step of the electrolyte needs to be removed multiple times, which may remove the silver atoms and/or silver nuclei in the electrolyte and affect the subsequent crystal growth step, so that the average particle size of the obtained silver nanoparticles is not within the expected range.

在一些實施例中,電解液可選擇性包含丙酮,丙酮可幫助微胞於電解液中分散更均勻,以利於銀核子生成。 In some embodiments, the electrolyte may optionally contain acetone, which can help disperse the micelles more evenly in the electrolyte to facilitate the generation of silver nuclei.

於操作110後,對電化學反應系統進行電化學反應,如操作120所示。具體而言,施加定電流至銀電極及相對電極,以電解銀電極成為複數個銀離子,且此些銀離子從相對電極接收電子後,生成複數個銀核子。此些銀核子可形成於粒徑控制試劑所形成之複數個微胞內部,以使 此些銀核子均勻分散於電解液中,從而利於後續藉由長晶時間製得具有不同平均粒徑之銀奈米粒子。附帶說明的是,如本發明所屬技術領域中具有通常知識者所能理解的,此些銀離子從相對電極接收電子後,可生成複數個銀核子,亦可生成複數個銀原子。 After operation 110, the electrochemical reaction system is subjected to an electrochemical reaction, as shown in operation 120. Specifically, a constant current is applied to the silver electrode and the opposite electrode to electrolyze the silver electrode into a plurality of silver ions, and these silver ions receive electrons from the opposite electrode to generate a plurality of silver nuclei. These silver nuclei can be formed inside a plurality of microcells formed by the particle size control reagent, so that these silver nuclei are uniformly dispersed in the electrolyte, thereby facilitating the subsequent production of silver nanoparticles with different average particle sizes by crystal growth time. It should be noted that, as can be understood by those with ordinary knowledge in the technical field to which the present invention belongs, these silver ions can generate a plurality of silver nuclei or a plurality of silver atoms after receiving electrons from the opposite electrode.

在一些實施例中,可施加90毫安培至110毫安培之定電流。此範圍內之定電流可更利於控制銀核子的生成數量。在控制銀核子的數量之情況下,可更易使後續長晶步驟的長晶速度更平穩,從而易於控制製得之銀奈米粒子的平均粒徑。 In some embodiments, a constant current of 90 mA to 110 mA can be applied. A constant current within this range can be more conducive to controlling the number of silver nuclei generated. When the number of silver nuclei is controlled, the growth rate of the subsequent crystal growth step can be more stable, thereby making it easier to control the average particle size of the produced silver nanoparticles.

在一些具體例中,電化學反應之反應時間為20秒至1分鐘,且較佳可為25秒至40秒,以利於生成銀核子,進而易於控制所製得之銀奈米粒子的平均粒徑。此外,較佳地,於電化學反應中,反應溫度可控制於28℃至32℃,此範圍內之溫度可使微胞更均勻分佈且更穩定地存在於電解液中,利於核控制試劑包覆銀核子,並使其尺寸較均一,從而更易於控制所製得之銀奈米粒子的平均粒徑。 In some specific examples, the reaction time of the electrochemical reaction is 20 seconds to 1 minute, and preferably 25 seconds to 40 seconds, so as to facilitate the generation of silver nuclei, and thus to facilitate the control of the average particle size of the produced silver nanoparticles. In addition, preferably, in the electrochemical reaction, the reaction temperature can be controlled at 28°C to 32°C. The temperature within this range can make the micelles more evenly distributed and more stably present in the electrolyte, which is conducive to the nuclear control reagent coating the silver nuclei and making their size more uniform, thereby making it easier to control the average particle size of the produced silver nanoparticles.

在較佳的實施例中,在電化學反應期間,可選擇性擾動電解液,以使銀核子均勻分散於微胞內部。前述之擾動電解液的方法可包含但不限於葉片式攪拌或超音波震盪,其中以超音波震盪為佳。舉例而言,超音波震盪可於電解液中產生大量氣穴爆破,故使銀離子及微胞快速均勻分佈於電解液中,從而助於銀核子之生成。 In a preferred embodiment, during the electrochemical reaction, the electrolyte can be selectively disturbed to evenly disperse the silver nuclei in the micelles. The aforementioned method of disturbing the electrolyte may include but is not limited to blade stirring or ultrasonic vibration, among which ultrasonic vibration is preferred. For example, ultrasonic vibration can produce a large number of cavitation explosions in the electrolyte, so that the silver ions and micelles are quickly and evenly distributed in the electrolyte, thereby helping the generation of silver nuclei.

於操作120後,停止施加定電流,並去除電解液 中粒徑控制試劑的一部份,直至粒徑控制試劑的濃度降低到3x10-8M至5x10-8M,以獲得長晶溶液,如操作130所示。詳述之,在生成銀核子後,停止施加定電流,以避免銀核子過度成長為不想要的大顆銀粒子(如平均粒徑大於10nm)。然後,利用如離心之方式去除電解液中部份的粒徑控制試劑。具體而言,前述離心的轉速可為16000rpm至20000rpm,且離心的時間可為20分鐘。 After operation 120, the application of the constant current is stopped, and a portion of the particle size control reagent in the electrolyte is removed until the concentration of the particle size control reagent is reduced to 3x10-8 M to 5x10-8 M to obtain a crystal growth solution, as shown in operation 130. In detail, after the silver nuclei are generated, the application of the constant current is stopped to prevent the silver nuclei from over-growing into unwanted large silver particles (such as an average particle size greater than 10nm). Then, a portion of the particle size control reagent in the electrolyte is removed by a method such as centrifugation. Specifically, the rotation speed of the centrifugation can be 16000rpm to 20000rpm, and the centrifugation time can be 20 minutes.

於前述去除之操作130中,降低粒徑控制試劑之濃度到3x10-8M至5x10-8M。倘若此濃度低於3x10-8M或高於5x10-8M,難以於同一長晶溶液中,藉由於特定長晶時間取出之部分而獲得特定平均粒徑之銀奈米粒子,其中前述之平均粒徑之分佈範圍可從25奈米至150奈米。 In the aforementioned removal operation 130, the concentration of the particle size control reagent is reduced to 3x10-8 M to 5x10-8 M. If the concentration is lower than 3x10-8 M or higher than 5x10-8 M, it is difficult to obtain silver nanoparticles of a specific average particle size from the same crystal growth solution by taking out a portion at a specific crystal growth time, wherein the aforementioned average particle size distribution ranges from 25 nm to 150 nm.

於操作130後,對此些銀核子進行長晶步驟,以獲得此些銀奈米粒子,如操作140所示。在長晶步驟中,此些銀核子之初始粒徑隨著長晶時間的增加而增大。舉例而言,長晶可由後述態樣達成:(1)多個銀核子聚集,(2)多個銀原子貼附於一個銀核子,(3)多個銀原子貼附於一個銀核子且此銀核子與其他銀核子聚集。為了簡化,上述態樣以「銀核子長晶」做概括性描述。從同一長晶溶液中,於特定的長晶時間取出長晶溶液之一部分,可獲得具有特定平均粒徑之銀奈米粒子,且前述平均粒徑之分佈範圍為25奈米至150奈米。因此,銀奈米粒子的製造方法100可於同一個長晶溶液中藉由不同的長晶時間製得多種平均粒徑之銀奈米粒子。換言之,相較於習知之銀奈米粒子的 製造方法,本發明之銀奈米粒子的製造方法100可利用同一種製造系統(即電化學反應系統)及相同的試劑(如粒徑控制試劑)生成銀核子,再於不同長晶時間取出電解液,即可獲得多種平均粒徑之銀奈米粒子,從而簡化製程並節省時間。 After operation 130, a crystal growth step is performed on these silver nuclei to obtain these silver nanoparticles, as shown in operation 140. In the crystal growth step, the initial particle size of these silver nuclei increases as the crystal growth time increases. For example, crystal growth can be achieved by the following aspects: (1) multiple silver nuclei aggregate, (2) multiple silver atoms attach to one silver nucleus, (3) multiple silver atoms attach to one silver nucleus and this silver nucleus aggregates with other silver nuclei. For simplicity, the above aspects are generally described as "silver nucleus crystal growth". By taking out a portion of the crystal growth solution at a specific crystal growth time from the same crystal growth solution, silver nanoparticles with a specific average particle size can be obtained, and the distribution range of the above-mentioned average particle size is 25 nanometers to 150 nanometers. Therefore, the method 100 for manufacturing silver nanoparticles can produce silver nanoparticles with a variety of average particle sizes in the same crystal growth solution by different crystal growth times. In other words, compared with the known method for manufacturing silver nanoparticles, the method 100 for manufacturing silver nanoparticles of the present invention can use the same manufacturing system (i.e., electrochemical reaction system) and the same reagent (such as particle size control reagent) to generate silver nuclei, and then take out the electrolyte at different crystal growth times to obtain silver nanoparticles with a variety of average particle sizes, thereby simplifying the process and saving time.

舉例而言,此些銀核子之初始粒徑可依據以下方程式(1)增大,以形成銀奈米粒子。 For example, the initial particle size of these silver nuclei can be enlarged according to the following equation (1) to form silver nanoparticles.

d=a+b×t (1) d = a + b × t (1)

於方程式(1)中,d代表銀核子之初始粒徑(奈米),且t代表長晶時間(小時)。 In equation (1), d represents the initial particle size of the silver nuclei (nanometers), and t represents the crystal growth time (hours).

在一些實施例中,當長晶時間短於8.3小時的時候,a代表之常數為27至28,b為10至10.5(奈米/小時)。在另一些實施例中,當長晶時間為8.3小時至98.5小時之間,a代表之常數為106至107,b為0.4至0.45(奈米/小時)。於是,根據以上方程式(1),可藉由長晶時間獲得多種平均粒徑之銀奈米粒子。較佳地,平均粒徑分佈範圍為28奈米至144奈米。 In some embodiments, when the crystal growth time is shorter than 8.3 hours, the constant represented by a is 27 to 28, and b is 10 to 10.5 (nm/hour). In other embodiments, when the crystal growth time is between 8.3 hours and 98.5 hours, the constant represented by a is 106 to 107, and b is 0.4 to 0.45 (nm/hour). Therefore, according to the above equation (1), silver nanoparticles with a variety of average particle sizes can be obtained by adjusting the crystal growth time. Preferably, the average particle size distribution ranges from 28 nm to 144 nm.

於操作140後,銀奈米粒子的製造方法100可選擇性包含終止步驟,藉由提高此些溶液中之粒徑控制試劑的濃度至大於0.15M,以停止銀核子的長晶步驟。詳述之,當粒徑控制試劑的濃度高於0.15M時,於前述長晶步驟中增大的銀核子(以下稱作銀粒子)之表面被粒徑控制試劑緊密包圍,所以粒徑控制試劑隔開相鄰之銀粒子,並阻止其繼續長晶而增大,以利於控制所製得之銀奈米粒子之 平均粒徑。 After operation 140, the method 100 for manufacturing silver nanoparticles may optionally include a termination step, by increasing the concentration of the particle size control reagent in these solutions to greater than 0.15M to stop the crystal growth step of the silver nuclei. Specifically, when the concentration of the particle size control reagent is higher than 0.15M, the surface of the silver nuclei (hereinafter referred to as silver particles) grown in the aforementioned crystal growth step is tightly surrounded by the particle size control reagent, so the particle size control reagent separates the adjacent silver particles and prevents them from continuing to grow and increase, so as to facilitate the control of the average particle size of the obtained silver nanoparticles.

以下利用實施例以說明本發明之應用,然其並非用以限定本發明,任何熟習此技藝者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾。 The following examples are used to illustrate the application of the present invention, but they are not used to limit the present invention. Anyone familiar with this technology can make various changes and modifications without departing from the spirit and scope of the present invention.

銀奈米粒子的製造 Production of silver nanoparticles

實施例1 Example 1

先提供電化學反應系統,其包含銀電極、相對電極、電解液及電力供應元件。電解液包含水、丙酮及十二烷基硫酸鈉,其中十二烷基硫酸鈉的濃度為0.1M。然後,對電解液施予超音波震盪(功率為120W且頻率為37kHz),並在30℃下,以100毫安培之定電流對電化學反應系統進行電化學反應,其反應時間為30秒。接續,停止施加定電流。之後,從電解液去除粒徑控制試劑,以降低其濃度至3.9x10-8M。接著,根據下表1所列之長晶時間分別從電解液取出複數個溶液,再額外加入十二烷基硫酸鈉,以提高其濃度至0.2M,從而停止銀核子繼續長晶。之後,藉由離心方式將長晶後之銀核子從電解液中分離出來,以獲得具有不同的平均粒徑之銀奈米粒子。 First, an electrochemical reaction system is provided, which includes a silver electrode, a counter electrode, an electrolyte and a power supply element. The electrolyte includes water, acetone and sodium dodecyl sulfate, wherein the concentration of sodium dodecyl sulfate is 0.1M. Then, ultrasonic vibration (power of 120W and frequency of 37kHz) is applied to the electrolyte, and the electrochemical reaction system is subjected to an electrochemical reaction at a constant current of 100 mA at 30°C for a reaction time of 30 seconds. Subsequently, the application of the constant current is stopped. Thereafter, the particle size control reagent is removed from the electrolyte to reduce its concentration to 3.9x10-8M . Next, multiple solutions were taken out from the electrolyte according to the crystal growth time listed in Table 1 below, and sodium dodecyl sulfate was added to increase its concentration to 0.2M, thereby stopping the silver nuclei from continuing to grow. Afterwards, the silver nuclei after crystal growth were separated from the electrolyte by centrifugation to obtain silver nanoparticles with different average particle sizes.

比較例1及2 Comparison Examples 1 and 2

比較例1及2之銀奈米粒子係以與實施例1相同的方法製備。不同的是,於去除操作中,比較例1及2分別降低十二烷基硫酸鈉的濃度到1.6x10-6M及9.8x10-10M。前述之實施例1及比較例1至2之具體條件及評價結果如下表1及圖2所示。 The silver nanoparticles of Comparative Examples 1 and 2 were prepared in the same manner as Example 1. The difference was that in the removal operation, the concentration of sodium dodecyl sulfate was reduced to 1.6x10 -6 M and 9.8x10 -10 M in Comparative Examples 1 and 2, respectively. The specific conditions and evaluation results of the aforementioned Example 1 and Comparative Examples 1 to 2 are shown in Table 1 and FIG. 2 below.

Figure 112102482-A0305-02-0012-1
Figure 112102482-A0305-02-0012-1

請參閱表1及圖2,圖2繪示實施例1及比較例1至2的銀核子之初始粒徑隨著長晶時間的增加而增大情形。於實施例1中,分別對0小時至8.3小時及8.3小時至96小時之長晶時間與相應之初始粒徑做線性回歸分析,以獲得於前述二個時段之回歸線的方程式,其分別如下方程式(1-1)及(1-2)所示。 Please refer to Table 1 and Figure 2. Figure 2 shows that the initial grain size of the silver nuclei in Example 1 and Comparative Examples 1 to 2 increases with the increase of the crystal growth time. In Example 1, linear regression analysis was performed on the crystal growth time from 0 hours to 8.3 hours and from 8.3 hours to 96 hours and the corresponding initial grain size to obtain the equations of the regression lines in the above two time periods, which are shown in the following equations (1-1) and (1-2) respectively.

d=27.43+10.25×t (1-1) d=27.43+10.25×t (1-1)

d=106.87+0.42×t (1-2) d=106.87+0.42×t (1-2)

於以上方程式(1-1)及(1-2)中,d代表銀核子的平均粒徑(奈米),且t代表長晶時間(小時)。 In the above equations (1-1) and (1-2), d represents the average particle size of silver nuclei (nanometers), and t represents the crystal growth time (hours).

於去除步驟中,實施例1降低十二烷基硫酸鈉濃度至3.9x10-8M(即適當濃度),故於同一個長晶溶液中製得之銀奈米粒子,其平均粒徑之分佈範圍可從28奈米至147奈米。此外,參照以上方程式(1-1)及(1-2),可於下一次製程中,於想要的平均粒徑所對應的長晶時間取出長晶溶液,進而獲得想要的平均粒徑之銀奈米粒子。 In the removal step, Example 1 reduces the concentration of sodium dodecyl sulfate to 3.9x10 -8 M (i.e., an appropriate concentration), so the average particle size distribution range of the silver nanoparticles produced in the same crystal growth solution can be from 28 nm to 147 nm. In addition, referring to the above equations (1-1) and (1-2), in the next process, the crystal growth solution can be taken out at the crystal growth time corresponding to the desired average particle size, thereby obtaining silver nanoparticles with the desired average particle size.

然而,請參閱圖2,於去除步驟中,比較例1降低十二烷基硫酸鈉濃度至1.6x10-6M,故僅能於同一個長晶 溶液中製得平均粒徑分佈範圍較窄之銀奈米粒子。另外,比較例2降低十二烷基硫酸鈉濃度至9.8x10-10M(即過低濃度),且由於多次移除十二烷基硫酸鈉,過程中一併移除電解液中之部分的銀核子及/或銀原子,以致不能於整個長晶過程中提供足夠的銀核子及/或銀原子,故僅能於同一個長晶溶液中製得平均粒徑分佈範圍更窄之銀奈米粒子。此外,由於十二烷基硫酸鈉濃度過低,無足夠的微胞可進行穩定的長晶,一部分的銀核子未被十二烷基硫酸鈉包圍,便直接快速聚集成過大顆的粒子而沉澱,所以量測平均粒徑時,沉澱的大顆粒子未被量測。 However, referring to FIG. 2 , in the removal step, the sodium dodecyl sulfate concentration is reduced to 1.6x10 -6 M in Comparative Example 1, so only silver nanoparticles with a narrower average particle size distribution range can be produced in the same crystal growth solution. In addition, the sodium dodecyl sulfate concentration is reduced to 9.8x10 -10 M (i.e., too low a concentration) in Comparative Example 2, and due to the multiple removals of sodium dodecyl sulfate, part of the silver nuclei and/or silver atoms in the electrolyte are removed during the process, so that sufficient silver nuclei and/or silver atoms cannot be provided in the entire crystal growth process, so only silver nanoparticles with a narrower average particle size distribution range can be produced in the same crystal growth solution. In addition, because the concentration of sodium dodecyl sulfate was too low, there were not enough micelles for stable crystal growth. Some silver nuclei were not surrounded by sodium dodecyl sulfate and aggregated into oversized particles and precipitated directly and quickly. Therefore, when measuring the average particle size, the precipitated large particles were not measured.

綜上所述,本發明之銀奈米粒子的製造方法係於高濃度的粒徑控制試劑之電解液下,利用電化學反應生成銀核子。再從電解液中移除粒徑控制試劑之一部分,以使銀核子於低濃度的粒徑控制試劑之電解液中長晶成銀奈米粒子,其中從同一長晶溶液於特定長晶時間取出之一部分,可獲得具有特定平均粒徑之銀奈米粒子,且銀奈米粒子之平均粒徑之分佈範圍為25奈米至150奈米,從而簡化製程並節省時間。 In summary, the method for manufacturing silver nanoparticles of the present invention utilizes electrochemical reaction to generate silver nuclei in an electrolyte solution with a high concentration of particle size control reagent. A portion of the particle size control reagent is then removed from the electrolyte solution, so that the silver nuclei grow into silver nanoparticles in an electrolyte solution with a low concentration of particle size control reagent. A portion of the solution taken out from the same crystal growth solution at a specific crystal growth time can obtain silver nanoparticles with a specific average particle size, and the average particle size distribution range of the silver nanoparticles is 25 nanometers to 150 nanometers, thereby simplifying the process and saving time.

雖然本發明已以實施方式揭露如上,然其並非用以限定本發明,在本發明所屬技術領域中任何具有通常知識者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed in the form of implementation as above, it is not intended to limit the present invention. Anyone with common knowledge in the technical field to which the present invention belongs can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the scope of protection of the present invention shall be subject to the scope of the patent application attached hereto.

100:方法 100:Methods

110,120,130,140:操作 110,120,130,140: Operation

Claims (10)

一種銀奈米粒子的製造方法,包含:提供一電化學反應系統,包含:一銀電極,做為一正極;一相對電極,做為一負極;一電解液,接觸該銀電極的一端及該相對電極的一端,其中該電解液包含一粒徑控制試劑,且該粒徑控制試劑之一濃度為0.08M至0.12M;以及一電力供應元件,分別電性連接該銀電極的另一端及該相對電極的另一端;對該電化學反應系統進行一電化學反應,其中施加一定電流至該銀電極及該相對電極,以電解該銀電極成為複數個銀離子,且該些銀離子從該相對電極接收電子後,生成複數個銀核子;停止施加該定電流,並去除該電解液中該粒徑控制試劑之一部分,直至該濃度降低到3x10-8M至5x10-8M,以獲得一長晶溶液;以及對該些銀核子進行一長晶步驟,以獲得該些銀奈米粒子,其中該些銀核子之一初始粒徑隨著一長晶時間的增加而增大,以形成該些銀奈米粒子,並且從同一該長晶溶液中,於特定的該長晶時間取出該長晶溶液之一部分,以獲得具有特定的一平均粒徑之該些銀奈米粒子,且該平均粒徑之一分佈範圍為25奈米至150奈米。 A method for manufacturing silver nanoparticles comprises: providing an electrochemical reaction system, comprising: a silver electrode, serving as a positive electrode; an opposite electrode, serving as a negative electrode; an electrolyte, contacting one end of the silver electrode and one end of the opposite electrode, wherein the electrolyte comprises a particle size control reagent, and a concentration of the particle size control reagent is 0.08M to 0.12M; and a power supply element, electrically connected to the silver electrode and the opposite electrode, respectively. The electrochemical reaction system is provided with a silver electrode and a counter electrode; an electrochemical reaction is performed on the silver electrode and the counter electrode, wherein a certain current is applied to the silver electrode and the counter electrode to electrolyze the silver electrode into a plurality of silver ions, and the silver ions generate a plurality of silver nuclei after receiving electrons from the counter electrode; the application of the certain current is stopped, and a portion of the particle size control reagent in the electrolyte is removed until the concentration is reduced to 3x10 -8 M to 5x10 -8 M to obtain a crystal growth solution; and performing a crystal growth step on the silver nuclei to obtain the silver nanoparticles, wherein an initial particle size of the silver nuclei increases with an increase in a crystal growth time to form the silver nanoparticles, and from the same crystal growth solution, a portion of the crystal growth solution is taken out at the specific crystal growth time to obtain the silver nanoparticles having a specific average particle size, and a distribution range of the average particle size is 25 nanometers to 150 nanometers. 如請求項1所述之銀奈米粒子的製造方法,其中該電解液更包含丙酮。 The method for manufacturing silver nanoparticles as described in claim 1, wherein the electrolyte further comprises acetone. 如請求項1所述之銀奈米粒子的製造方法,其中該粒徑控制試劑包含十二烷基硫酸鈉。 A method for producing silver nanoparticles as described in claim 1, wherein the particle size control reagent contains sodium dodecyl sulfate. 如請求項1所述之銀奈米粒子的製造方法,其中該定電流為90毫安培至110毫安培。 The method for manufacturing silver nanoparticles as described in claim 1, wherein the constant current is 90 mA to 110 mA. 如請求項1所述之銀奈米粒子的製造方法,其中該電化學反應之一反應時間為20秒至1分鐘。 The method for manufacturing silver nanoparticles as described in claim 1, wherein a reaction time of the electrochemical reaction is 20 seconds to 1 minute. 如請求項1所述之銀奈米粒子的製造方法,其中該電化學反應之一反應溫度為28℃至32℃。 The method for manufacturing silver nanoparticles as described in claim 1, wherein a reaction temperature of the electrochemical reaction is 28°C to 32°C. 如請求項1所述之銀奈米粒子的製造方法,其中在該電化學反應期間,擾動該電解液。 A method for manufacturing silver nanoparticles as described in claim 1, wherein the electrolyte is disturbed during the electrochemical reaction. 如請求項1所述之銀奈米粒子的製造方法,其中於該電化學反應中,該些銀核子生成於該粒徑控制試劑所形成之複數個微胞內部。 The method for producing silver nanoparticles as described in claim 1, wherein in the electrochemical reaction, the silver nuclei are generated inside a plurality of micelles formed by the particle size control reagent. 如請求項1所述之銀奈米粒子的製造方法, 其中於該長晶步驟中,該初始粒徑係依據方程式(1)而增大:d=a+b×t (1),於該方程式(1)中,a代表常數,d代表該初始粒徑(奈米),t代表該長晶時間(小時),並且當該長晶時間短於8.3小時的時候,a為27至28,b為10至10.5(奈米/小時),或者當該長晶時間為8.3小時至98.5小時之間,a為106至107,b為0.4至0.45(奈米/小時)。 A method for manufacturing silver nanoparticles as described in claim 1, wherein in the crystal growth step, the initial particle size increases according to equation (1): d = a + b × t (1), in which a represents a constant, d represents the initial particle size (nanometers), t represents the crystal growth time (hours), and when the crystal growth time is shorter than 8.3 hours, a is 27 to 28, and b is 10 to 10.5 (nanometers/hour), or when the crystal growth time is between 8.3 hours and 98.5 hours, a is 106 to 107, and b is 0.4 to 0.45 (nanometers/hour). 如請求項1所述之銀奈米粒子的製造方法,其中於該長晶步驟後,該銀奈米粒子的製造方法更包含一終止步驟,藉由提高該些溶液中之該粒徑控制試劑之一濃度至大於0.15M,以停止該長晶步驟。 The method for producing silver nanoparticles as described in claim 1, wherein after the crystal growth step, the method for producing silver nanoparticles further comprises a termination step, by increasing the concentration of the particle size control reagent in the solutions to greater than 0.15M to stop the crystal growth step.
TW112102482A 2023-01-19 2023-01-19 Method for producing silver nanoparticles TWI842351B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW112102482A TWI842351B (en) 2023-01-19 2023-01-19 Method for producing silver nanoparticles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW112102482A TWI842351B (en) 2023-01-19 2023-01-19 Method for producing silver nanoparticles

Publications (2)

Publication Number Publication Date
TWI842351B true TWI842351B (en) 2024-05-11
TW202430722A TW202430722A (en) 2024-08-01

Family

ID=92076807

Family Applications (1)

Application Number Title Priority Date Filing Date
TW112102482A TWI842351B (en) 2023-01-19 2023-01-19 Method for producing silver nanoparticles

Country Status (1)

Country Link
TW (1) TWI842351B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8282860B2 (en) * 2006-08-07 2012-10-09 Inktec Co., Ltd. Process for preparation of silver nanoparticles, and the compositions of silver ink containing the same
CN106270543A (en) * 2015-06-12 2017-01-04 中国科学院大连化学物理研究所 The method preparing the controlled Triangular nanoplates of arrangement mode continuously
US20170259341A1 (en) * 2016-03-09 2017-09-14 King Abdulaziz University Method of forming silver nanoparticles and a use thereof
CN114101656A (en) * 2021-12-07 2022-03-01 浙江大学 Preparation method and application of silver nanoparticles with universal dispersion characteristics

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8282860B2 (en) * 2006-08-07 2012-10-09 Inktec Co., Ltd. Process for preparation of silver nanoparticles, and the compositions of silver ink containing the same
CN106270543A (en) * 2015-06-12 2017-01-04 中国科学院大连化学物理研究所 The method preparing the controlled Triangular nanoplates of arrangement mode continuously
US20170259341A1 (en) * 2016-03-09 2017-09-14 King Abdulaziz University Method of forming silver nanoparticles and a use thereof
CN114101656A (en) * 2021-12-07 2022-03-01 浙江大学 Preparation method and application of silver nanoparticles with universal dispersion characteristics

Similar Documents

Publication Publication Date Title
CN112723422B (en) Aluminum-doped cobaltosic oxide core-shell material and preparation method thereof
Zhang et al. Hierarchical Self‐assembly of Microscale Cog‐like Superstructures for Enhanced Performance in Lithium‐Ion Batteries
CN114180644B (en) Aluminum-doped cobalt carbonate material, preparation method thereof, aluminum-doped cobaltosic oxide and lithium cobaltate positive electrode material
CN104779388A (en) Nickel and cobalt binary anode material precursor preparing method and nickel and cobalt binary anode material precursor prepared through method
CN106711419B (en) The porous composite lithium ion battery cathode material of the NiO/C of core-shell structure copolymer shape
Mackay et al. Template-free electrochemical synthesis of tin nanostructures
CN108899550B (en) Composite coated positive electrode active material, preparation method thereof, lithium ion battery positive electrode material and solid-state lithium ion battery
US20210354990A1 (en) Porous graphene film, its manufacturing method and electronic product
CN108390048B (en) Nitrogen-phosphorus co-doped carbon-coated MoO3-x and preparation method thereof
JP2018531322A (en) Method for producing novel silver nanowires with uniform aspect ratio and nodes
JP2018531322A6 (en) Method for producing novel silver nanowires with uniform aspect ratio and nodes
Yu et al. A novel strategy to electrodeposit high-quality copper foils using composite additive and pulse superimposed on direct current
TW201834973A (en) Nickel Cobalt Sulfide Synthesizing Method and Electrode
CN114645329B (en) Nickel-cobalt-manganese hydroxide with high nickel and low cobalt fine whisker and preparation method thereof
CN112968173A (en) Porous carbon-coated sulfur vacancy composite electrode material, preparation method thereof and circular electrode adopting material
TWI842351B (en) Method for producing silver nanoparticles
CN109321948B (en) Method for preparing silver nanorods by rapid green electrochemical method
CN116514180A (en) Ternary precursor material, preparation method, ternary positive electrode material and lithium ion battery
Du et al. Electrochemical performances of LiNi0. 83Co0. 12Mn0. 05O2 by dual doping of Mg and Ti
Islam et al. Study of structural and optical properties of electrodeposited silicon films on graphite substrates
Wang et al. Nickel‐Based Sulfide Materials for Batteries
TW202430722A (en) Method for producing silver nanoparticles
CN113798504A (en) Preparation method of rare earth oxide dispersion-enhanced tungsten powder for 3D printing
Chang et al. Large-scale production of tungsten trioxide nanoparticles for electrochromic application
CN116588993A (en) Ternary precursor, preparation method thereof, lithium battery positive electrode material and lithium battery