TWI704109B - Method of recovering gold using thiourea graphene - Google Patents

Method of recovering gold using thiourea graphene Download PDF

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TWI704109B
TWI704109B TW108134030A TW108134030A TWI704109B TW I704109 B TWI704109 B TW I704109B TW 108134030 A TW108134030 A TW 108134030A TW 108134030 A TW108134030 A TW 108134030A TW I704109 B TWI704109 B TW I704109B
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graphene
thiourea
ions
gold
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TW202112675A (en
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席行正
陳煜偈
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國立臺灣大學
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Abstract

A method of recovering gold using thiourea graphene includes the following steps. Providing a thiourea graphene. The thiourea graphene is added to the wastewater to carry out an adsorption reaction. The wastewater includes at least gold ions, and the thiourea graphene selectively adsorbs the gold ions. The thiourea graphene adsorbing the gold ions is separated from the wastewater. The thiourea graphene adsorbing the gold ions is subjected to a desorption reaction to obtain an aqueous solution containing the gold ions.

Description

使用硫脲石墨烯之回收金的方法Method for recovering gold using thiourea graphene

本發明是有關於一種回收金的方法,且特別是有關於一種使用硫脲石墨烯之回收金的方法。The present invention relates to a method for recovering gold, and particularly to a method for recovering gold using thiourea graphene.

目前,從廢水中回收金之方法,是以離子交換樹脂作為吸附材的方法為主,其相較於傳統的電解法,較能符合環保節能的趨勢,且同時具有良好的吸附效率以及回收率。然而,離子交換樹脂在硝酸體系中卻無法產生作用,且其對於金離子之最低吸附極限只有1毫克/公升。因此,當廢水中的金離子濃度低於1毫克/公升時,離子交換樹脂對於金離子的吸效附效率則會明顯變差。At present, the method of recovering gold from waste water is mainly based on ion exchange resin as the adsorption material. Compared with the traditional electrolysis method, it is more in line with the trend of environmental protection and energy saving, and has good adsorption efficiency and recovery rate. . However, ion-exchange resin has no effect in the nitric acid system, and its minimum adsorption limit for gold ions is only 1 mg/liter. Therefore, when the concentration of gold ions in the wastewater is less than 1 mg/liter, the absorption efficiency of the ion exchange resin for gold ions will be significantly worse.

本發明提供一種使用硫脲石墨烯之回收金的方法,利用硫脲石墨烯對於金離子的高選擇性,使得使用硫脲石墨烯之回收金的方法可具有較低的吸附極限、較佳的吸附效率以及較高的飽和吸附容量。The present invention provides a gold recovery method using thiourea graphene, which utilizes the high selectivity of thiourea graphene for gold ions, so that the gold recovery method using thiourea graphene can have a lower adsorption limit and better Adsorption efficiency and higher saturated adsorption capacity.

本發明的使用硫脲石墨烯之回收金的方法包括以下步驟。首先,提供硫脲石墨烯。接著,將硫脲石墨烯加入至廢水中,以進行吸附反應。其中,廢水至少包括金離子,且硫脲石墨烯會選擇性吸附金離子。而後,將吸附金離子的硫脲石墨烯與廢水分離。最後,對吸附金離子的硫脲石墨烯進行脫附反應,以得到含有金離子的溶液。The method for recovering gold using thiourea graphene of the present invention includes the following steps. First, provide thiourea graphene. Next, graphene thiourea is added to the wastewater to perform an adsorption reaction. Among them, the wastewater includes at least gold ions, and thiourea graphene can selectively adsorb gold ions. Then, the thiourea graphene that adsorbs gold ions is separated from the wastewater. Finally, the thiourea graphene adsorbing gold ions is subjected to a desorption reaction to obtain a solution containing gold ions.

在本發明的一實施例中,上述的硫脲石墨烯的氮含量為2~4重量%且硫含量為20~23重量%。In an embodiment of the present invention, the nitrogen content of the above-mentioned thiourea graphene is 2 to 4% by weight and the sulfur content is 20 to 23% by weight.

在本發明的一實施例中,上述的硫脲石墨烯為0.5毫克至2.0毫克。In an embodiment of the present invention, the above-mentioned thiourea graphene is 0.5 mg to 2.0 mg.

在本發明的一實施例中,上述的吸附反應的反應條件包括:pH值為2至6,反應時間為96小時以上。In an embodiment of the present invention, the reaction conditions of the aforementioned adsorption reaction include: a pH value of 2 to 6 and a reaction time of more than 96 hours.

在本發明的一實施例中,上述的廢水的金離子的濃度為0.01毫克/公升至10毫克/公升。In an embodiment of the present invention, the concentration of gold ions in the wastewater is 0.01 mg/liter to 10 mg/liter.

在本發明的一實施例中,上述的硫脲石墨烯對金離子的吸附效率為95%至100%。In an embodiment of the present invention, the above-mentioned thiourea graphene has an adsorption efficiency of 95% to 100% for gold ions.

在本發明的一實施例中,上述當廢水更包括銅離子、鉛離子、鋅離子或其組合時,硫脲石墨烯對鉛離子的吸附效率為1%至2%,且對銅離子及鋅離子的吸附效率為0%。In an embodiment of the present invention, when the wastewater further includes copper ions, lead ions, zinc ions, or a combination thereof, the adsorption efficiency of thiourea graphene for lead ions is 1% to 2%, and the adsorption efficiency for copper ions and zinc The adsorption efficiency of ions is 0%.

在本發明的一實施例中,上述的每克硫脲石墨烯對金離子的飽和吸附容量為833.33毫克。In an embodiment of the present invention, the above-mentioned saturated adsorption capacity of gold ions per gram of thiourea graphene is 833.33 mg.

在本發明的一實施例中,上述對吸附金離子的硫脲石墨烯進行脫附反應的步驟包括:將脫附劑加入於吸附金離子的硫脲石墨烯中,以使金離子從硫脲石墨烯上脫附。In an embodiment of the present invention, the step of performing the desorption reaction on the thiourea graphene adsorbing gold ions includes: adding a desorbent to the thiourea graphene adsorbing gold ions, so that the gold ions are removed from the thiourea graphene Desorption on graphene.

在本發明的一實施例中,上述的金離子的脫附效率為93%至96%。In an embodiment of the present invention, the aforementioned gold ion desorption efficiency is 93% to 96%.

基於上述,在本發明提供的使用硫脲石墨烯之回收金的方法中,藉由硫脲石墨烯對於金離子的高選擇性,使得在利用硫脲石墨烯對廢水中的金離子進行吸附反應時,可具有較低的吸附極限、較佳的吸附效率以及較高的飽和吸附容量。Based on the above, in the method for recovering gold using thiourea graphene provided by the present invention, the high selectivity of thiourea graphene for gold ions enables the use of thiourea graphene to adsorb gold ions in wastewater. It can have a lower adsorption limit, better adsorption efficiency and higher saturated adsorption capacity.

為讓本發明的上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。In order to make the above-mentioned features and advantages of the present invention more comprehensible, the following specific embodiments are described in detail in conjunction with the accompanying drawings.

圖1繪示為本發明一實施例的一種硫脲石墨烯之回收金的方法的流程圖。FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention.

請參照圖1,進行步驟S110,提供硫脲石墨烯。在本實施例中,例如是以以下步驟來製備硫脲石墨烯,但不以此為限。首先,將氧化石墨烯(graphene oxide,GO)與超純水(ultrapure water)混合以形成氧化石墨烯的膠體懸浮液。將硫脲溶解在超純水中,以形成硫脲溶液。然後,將硫脲溶液加入於氧化石墨烯的膠體懸浮液中,以磁力攪拌棒在95°C下進行攪拌8小時,以形成硫脲石墨烯(thiourea graphene,TU-rGO)。隨後,用超純水洗滌TU-rGO溶液並過濾,以獲得硫脲石墨烯固體。最後,在將固體於50℃下乾燥24小時後,以瑪瑙研缽對硫脲石墨烯固體進行研磨。接著,依序通過30目篩(mesh sieve)以及60目篩,以獲得粒徑在0.25毫米至0.59毫米之間的硫脲石墨烯。Please refer to FIG. 1 to perform step S110 to provide thiourea graphene. In this embodiment, for example, the following steps are used to prepare thiourea graphene, but it is not limited thereto. First, graphene oxide (GO) is mixed with ultrapure water to form a colloidal suspension of graphene oxide. Dissolve thiourea in ultrapure water to form a thiourea solution. Then, the thiourea solution was added to the colloidal suspension of graphene oxide, and stirred with a magnetic stir bar at 95° C. for 8 hours to form thiourea graphene (TU-rGO). Subsequently, the TU-rGO solution was washed with ultrapure water and filtered to obtain thiourea graphene solids. Finally, after drying the solid at 50° C. for 24 hours, the thiourea graphene solid was ground with an agate mortar. Then, pass through a 30-mesh sieve and a 60-mesh sieve in sequence to obtain thiourea graphene with a particle size between 0.25 mm and 0.59 mm.

接著,對氧化石墨烯以及硫脲石墨烯中的元素成份及其含量進行分析,其結果如表1所示。Next, the elemental components and contents in graphene oxide and graphene thiourea were analyzed, and the results are shown in Table 1.

表1   C (%) O (%) H (%) N (%) S (%) GO 47.21±0.01 39.99±1.70 2.75±0.08 0.13±0.02 3.72±0.00 TU-rGO 60.38±1.22 10.00±0.08 1.05±0.10 2.01±0.22 22.87±0.34 Table 1 C (%) O (%) H (%) N (%) S (%) GO 47.21±0.01 39.99±1.70 2.75±0.08 0.13±0.02 3.72±0.00 TU-rGO 60.38±1.22 10.00±0.08 1.05±0.10 2.01±0.22 22.87±0.34

由表1的結果可知,相較於氧化石墨烯,硫脲石墨烯的氮含量及硫含量分別增加至2.01%以及22.87%,且氧含量減少至10.00%。表示硫脲石墨烯是藉由取代氧的方式來增加氮、硫的含量。From the results in Table 1, it can be seen that compared with graphene oxide, the nitrogen content and sulfur content of thiourea graphene increased to 2.01% and 22.87%, respectively, and the oxygen content decreased to 10.00%. It means that graphene thiourea increases the content of nitrogen and sulfur by replacing oxygen.

接著,由圖2A的X光繞射的分析結果可知,相較於石墨烯的繞射峰位置(2θ=26.5°)以及氧化石墨烯的繞射峰位置(2θ= 26.5°或10.5°),硫脲石墨烯具有的繞射峰位置為2θ = 23.05°。Next, from the X-ray diffraction analysis result of Fig. 2A, it can be seen that, compared to the diffraction peak position of graphene (2θ=26.5°) and the diffraction peak position of graphene oxide (2θ=26.5° or 10.5°), The diffraction peak position of thiourea graphene is 2θ = 23.05°.

由圖2B的掃瞄式電子顯微鏡的分析結果可知,在3000倍的放大圖中,硫脲石墨烯的表面具有高度折疊的結構。由圖2C的穿透式電子顯微鏡的分析結果可知,在60000倍的放大圖中,硫脲石墨烯具有多層結構,且測得的比表面積為4.5 m 2/g。 From the analysis result of the scanning electron microscope in FIG. 2B, it can be seen that the surface of the graphene thiourea has a highly folded structure in a magnified view of 3000 times. From the analysis result of the transmission electron microscope in FIG. 2C, it can be seen that in the 60,000 times magnification, the thiourea graphene has a multilayer structure, and the measured specific surface area is 4.5 m 2 /g.

接著,進行步驟S120,將硫脲石墨烯加入至廢水中,以進行吸附反應。在本實施例中,廢水至少包括金離子。Then, step S120 is performed to add thiourea graphene to the wastewater to perform an adsorption reaction. In this embodiment, the wastewater includes at least gold ions.

以下將以不同的實施例來探討硫脲石墨烯對廢水中的金離子進行吸附反應的反應條件。In the following, different examples will be used to discuss the reaction conditions for the adsorption reaction of thiourea graphene to gold ions in wastewater.

實施例Example 11 :反應時間對吸附效率的影響:The influence of reaction time on adsorption efficiency

在本實施例中,反應條件為:硫脲石墨烯為0.5毫克、金離子的濃度為10毫克/公升、反應溫度為30℃、振盪速度為150 rpm、pH值為2、反應體積為50毫升,且反應時間分別為12、24、48、72、96、120小時。In this embodiment, the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50 ml. , And the reaction time is 12, 24, 48, 72, 96, 120 hours.

由圖3A的結果可知,當反應時間為96小時,硫脲石墨烯對金離子的吸附效率約為82.7±6.1%。當反應時間為120小時,硫脲石墨烯對金離子的吸附效率則沒有顯著地增加。也就是說,當反應時間為96小時,硫脲石墨烯對金離子的吸附動力學可達到一平衡,且可以展現不錯地吸附效率。It can be seen from the result of Figure 3A that when the reaction time is 96 hours, the adsorption efficiency of thiourea graphene for gold ions is about 82.7±6.1%. When the reaction time is 120 hours, the adsorption efficiency of thiourea graphene for gold ions does not increase significantly. That is to say, when the reaction time is 96 hours, the adsorption kinetics of thiourea graphene to gold ions can reach an equilibrium, and can exhibit good adsorption efficiency.

須要說明的是,在本實施例中,吸附效率是依據公式1來計算。公式1:吸附效率(%)=(C 0-C t)/C 0×100%,其中C 0為吸附反應前的金離子濃度(毫克/公升),C t為吸附反應後的金離子濃度(毫克/公升)。 It should be noted that in this embodiment, the adsorption efficiency is calculated according to Formula 1. Formula 1: Adsorption efficiency (%)=(C 0 -C t )/C 0 ×100%, where C 0 is the gold ion concentration before the adsorption reaction (mg/liter), and C t is the gold ion concentration after the adsorption reaction (Mg/liter).

實施例Example 22 :反應的:react pHpH 值對吸附Value pair adsorption 效率的影響The impact of efficiency

在本實施例中,反應條件為:硫脲石墨烯為0.5毫克、金離子的濃度為10毫克/公升、反應溫度為30℃、振盪速度為150 rpm、反應時間為96小時、反應體積為50毫升,且反應的pH值分別為2、3、4、5、6、7、8、9、10。In this example, the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the reaction time is 96 hours, and the reaction volume is 50. Milliliters, and the pH values of the reaction were 2, 3, 4, 5, 6, 7, 8, 9, 10, respectively.

由圖3B的結果可知,當反應的pH值為2~5時,硫脲石墨烯對金離子的吸附效率約為80~85%。當反應的pH值為6時,硫脲石墨烯對金離子的吸附效率約為40~50%。然而,當反應的pH值超過6時,硫脲石墨烯對金離子的吸附效率則快速地降低至20%以下。也就是說,當反應的pH值為2~5時,硫脲石墨烯對金離子都可以展現不錯地吸附效率。It can be seen from the results of Figure 3B that when the pH of the reaction is 2~5, the adsorption efficiency of thiourea graphene for gold ions is about 80~85%. When the pH of the reaction is 6, the adsorption efficiency of thiourea graphene for gold ions is about 40-50%. However, when the pH of the reaction exceeds 6, the adsorption efficiency of thiourea graphene for gold ions quickly drops below 20%. In other words, when the pH of the reaction is 2~5, thiourea graphene can exhibit good adsorption efficiency for gold ions.

實施例Example 33 :硫脲石墨烯的劑量對吸附效率的影響:The influence of the dosage of thiourea graphene on the adsorption efficiency

在本實施例中,反應條件為:金離子的濃度為10毫克/公升、反應溫度為30℃、振盪速度為150 rpm、反應時間為96小時、反應體積為50毫升、pH值為5,且硫脲石墨烯的劑量分別為0.5、1.0、1.5、2.0毫克。In this embodiment, the reaction conditions are: the concentration of gold ions is 10 mg/liter, the reaction temperature is 30° C., the shaking speed is 150 rpm, the reaction time is 96 hours, the reaction volume is 50 ml, the pH is 5, and The dosage of thiourea graphene is 0.5, 1.0, 1.5, 2.0 mg, respectively.

由圖3C的結果可知,當硫脲石墨烯的劑量為0.5毫克時,硫脲石墨烯對金離子的吸附效率約為82.7±6.1%。然而,當硫脲石墨烯的劑量為1.0、1.5或2.0毫克時,硫脲石墨烯對金離子的吸附效率只有些微地增加。也就是說,當硫脲石墨烯的劑量為0.5~2.0毫克時,其對金離子都可以展現不錯地吸附效率。It can be seen from the results of Figure 3C that when the dose of thiourea graphene is 0.5 mg, the adsorption efficiency of thiourea graphene for gold ions is about 82.7±6.1%. However, when the dose of thiourea graphene is 1.0, 1.5, or 2.0 mg, the adsorption efficiency of thiourea graphene for gold ions only slightly increases. In other words, when the dosage of thiourea graphene is 0.5 to 2.0 mg, it can show good adsorption efficiency for gold ions.

然後,進行步驟S130,將吸附金離子的硫脲石墨烯與廢水分離。在本實施例中,在硫脲石墨烯吸附廢水中的金離子之後,例如是以孔洞大小為0.45微米的針筒過濾器(Syringe filter)進行過濾,以使反應後的硫脲石墨烯無法通過孔洞,進而將吸附金離子的硫脲石墨烯與反應後的廢水分離。接著,以感應耦合電漿放射光譜儀(Inductively Couple Plasma Optical Emission Spectrometry,ICP-OES)量測分離後的廢水中的金離子濃度,以作為公式1中的反應後的金離子濃度。Then, step S130 is performed to separate the thiourea graphene adsorbing gold ions from the wastewater. In this embodiment, after the thiourea graphene adsorbs the gold ions in the wastewater, for example, it is filtered with a Syringe filter with a pore size of 0.45 microns, so that the reacted thiourea graphene cannot pass through. The pores further separate the thiourea graphene adsorbing gold ions from the wastewater after the reaction. Next, an inductively coupled plasma emission spectrometer (ICP-OES) is used to measure the gold ion concentration in the separated wastewater, which is used as the gold ion concentration after the reaction in Formula 1.

最後,進行步驟S140,對吸附金離子的硫脲石墨烯進行脫附反應,以得到金離子。在本實施例中,例如是將脫附劑加入於上述與反應後的廢水分離且吸附有金離子的硫脲石墨烯中,以使金離子可從硫脲石墨烯上脫附。在本實施例中,脫附劑例如是硫代硫酸銨(ammonium thiosulfate),但不以此為限。Finally, step S140 is performed to perform a desorption reaction on the thiourea graphene adsorbing gold ions to obtain gold ions. In this embodiment, for example, a desorbent is added to the thiourea graphene separated from the wastewater after the reaction and adsorbed with gold ions, so that the gold ions can be desorbed from the thiourea graphene. In this embodiment, the desorption agent is, for example, ammonium thiosulfate, but it is not limited to this.

以下將以不同的實施例來探討硫代硫酸銨對吸附有金離子的硫脲石墨烯進行脫附反應的反應條件。In the following, different examples will be used to discuss the reaction conditions for the desorption reaction of thiourea graphene with gold ions adsorbed by ammonium thiosulfate.

實施例Example 44 :硫代硫酸銨溶液的濃度對脫附效率的影響:The influence of the concentration of ammonium thiosulfate solution on the desorption efficiency

在本實施例中,依據所使用的硫代硫酸銨溶液的濃度分為A、B、C三組,且每組皆進行兩次脫附反應。首先,每組皆在2.0毫克吸附有金離子的硫脲石墨烯(每克硫脲石墨烯所吸附的金離子的含量為2500毫克)中加入0.2M的硫代硫酸銨溶液,以進行第一次脫附反應。接著,在進行完第一次脫附反應之後,A、B、C三組分別以0.05、0.1或0.2M的硫代硫酸銨溶液進行第二次脫附反應。此外,第一次脫附反應與第二次脫附反應皆依據以下的反應條件進行:反應溫度為30℃、振盪速度為150 rpm、反應時間為24小時、反應體積為50毫升、反應的pH值分別為7.4。In this embodiment, the concentration of the ammonium thiosulfate solution used is divided into three groups, A, B, and C, and each group performs two desorption reactions. First, each group adds 0.2M ammonium thiosulfate solution to 2.0 mg of thiourea graphene with gold ions adsorbed (the content of gold ions adsorbed per gram of thiourea graphene is 2500 mg) to perform the first Second desorption reaction. Then, after the first desorption reaction is completed, the three groups A, B, and C are respectively used for the second desorption reaction with 0.05, 0.1 or 0.2M ammonium thiosulfate solution. In addition, the first desorption reaction and the second desorption reaction are carried out according to the following reaction conditions: reaction temperature is 30°C, shaking speed is 150 rpm, reaction time is 24 hours, reaction volume is 50 ml, reaction pH The values are 7.4 respectively.

由圖3D的結果可知,第一次脫附反應就可以使大部分的金離子從硫脲石墨烯上脫附,且具有約93%以上的脫附效率。而在第二次脫附反應中,以0.2M的硫代硫酸銨溶液(C組)可再增加約1.4%的脫附效率。也就是說,以硫代硫酸銨溶液進行脫附反應,可以使硫脲石墨烯上的金離子脫附的脫附效率為93%至96%。From the results in Figure 3D, it can be seen that the first desorption reaction can desorb most of the gold ions from the thiourea graphene, and the desorption efficiency is over 93%. In the second desorption reaction, 0.2M ammonium thiosulfate solution (group C) can increase the desorption efficiency by about 1.4%. In other words, the desorption reaction with ammonium thiosulfate solution can make the desorption efficiency of gold ions on the thiourea graphene be 93% to 96%.

須要說明的是,在本實施例中,脫附效率是依據公式2來計算。公式2:脫附效率(%)=M t/M 0×100%,其中M 0為脫附反應前的硫脲石墨烯上的金離子的重量(毫克),C t為脫附反應後的金離子於溶液中的重量(毫克)。 It should be noted that in this embodiment, the desorption efficiency is calculated according to Formula 2. Formula 2: Desorption efficiency (%)=M t /M 0 ×100%, where M 0 is the weight (mg) of gold ions on the thiourea graphene before the desorption reaction, and C t is the weight after the desorption reaction The weight of gold ions in solution (mg).

值得說明的是,為了進一步得知硫脲石墨烯對金離子的吸附效果,可將上述實施例的實驗數據套用至Langmuir吸附方程式中,以進行等溫吸附曲線之模擬,其結果如圖4所示。由圖4的模擬結果可知,等溫吸附曲線的相關係數(correlation coefficient)R 2為0.91,且每克硫脲石墨烯對金離子的飽和吸附容量為833.33毫克。 It is worth noting that, in order to further understand the adsorption effect of thiourea graphene on gold ions, the experimental data of the above examples can be applied to the Langmuir adsorption equation to simulate the adsorption isotherm curve. The results are shown in Figure 4. Show. It can be seen from the simulation result of FIG. 4 that the correlation coefficient R 2 of the adsorption isotherm curve is 0.91, and the saturated adsorption capacity of gold ions per gram of thiourea graphene is 833.33 mg.

由於上述吸附實驗皆以金離子的濃度為10毫克/公升為例,但真實環境的廢水中,其金離子的濃度可能比10毫克/公升還低,且可能同時含有其他的金屬離子,例如銅離子、鉛離子、鋅離子或其組合。因此,以下將以不同的實施例來探討硫脲石墨烯對金離子的最低可吸附濃度,並探討硫脲石墨烯對金離子和其他金屬離子的選擇性。Since the above adsorption experiments all take the gold ion concentration of 10 mg/liter as an example, the concentration of gold ions in the wastewater in the real environment may be lower than 10 mg/liter, and may also contain other metal ions, such as copper. Ion, lead ion, zinc ion, or a combination thereof. Therefore, in the following, different examples will be used to discuss the minimum adsorbable concentration of thiourea graphene for gold ions, and to discuss the selectivity of thiourea graphene for gold ions and other metal ions.

實施例Example 55 :比較氧化石墨烯與硫脲石墨烯,其分別對金離子、銅離子、鉛離子及鋅離子的吸附效率:Comparing graphene oxide and graphene thiourea, respectively, the adsorption efficiency of gold ion, copper ion, lead ion and zinc ion

在本實施例中,以2.0毫克的氧化石墨烯(或2.0毫克的硫脲石墨烯)分別與濃度為10毫克/公升的金離子(標示為Au)、濃度為20毫克/公升的銅離子(標示為Cu)、濃度為20毫克/公升的鉛離子(標示為Pb)、濃度為20毫克/公升的鋅離子(標示為Zn)進行吸附反應,且其反應條件為:反應溫度為30℃、振盪速度為150 rpm、pH值為2、反應體積為50毫升、反應時間為96小時。In this embodiment, 2.0 mg of graphene oxide (or 2.0 mg of thiourea graphene) is used with gold ions (denoted as Au) at a concentration of 10 mg/liter and copper ions at a concentration of 20 mg/liter ( The adsorption reaction is carried out with lead ions with a concentration of 20 mg/liter (marked as Pb) and zinc ions with a concentration of 20 mg/liter (marked as Zn), and the reaction conditions are: reaction temperature of 30°C, The shaking speed is 150 rpm, the pH is 2, the reaction volume is 50 ml, and the reaction time is 96 hours.

由圖5A的結果可知,氧化石墨烯對金離子的吸附效率約為12%,硫脲石墨烯對金離子的吸附效率約為98%,且硫脲石墨烯對銅離子、鉛離子及鋅離子皆不具有吸附效率。因此,相較於氧化石墨烯,硫脲石墨烯對金離子具有較高的吸附效率。此外,相較於銅離子、鉛離子及鋅離子,硫脲石墨烯對金離子具有高選擇性。From the result of Figure 5A, it can be seen that the adsorption efficiency of graphene oxide on gold ions is about 12%, the adsorption efficiency of thiourea graphene on gold ions is about 98%, and the adsorption efficiency of thiourea graphene on copper ions, lead ions and zinc ions None have adsorption efficiency. Therefore, compared with graphene oxide, graphene thiourea has a higher adsorption efficiency for gold ions. In addition, compared with copper ions, lead ions and zinc ions, thiourea graphene has high selectivity to gold ions.

實施例Example 66 :硫脲石墨烯對廢水中的金離子、銅離子、鉛離子及鋅離子的選擇性:The selectivity of thiourea graphene to gold ion, copper ion, lead ion and zinc ion in wastewater

在本實施例中,依據廢水的組成成份及其含量分為實驗例1、實驗例2以及實驗例3。其中,實驗例1的廢水包括濃度為10毫克/公升的金離子、濃度為20毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例2的廢水包括濃度為1毫克/公升的金離子、濃度為20毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例3的廢水包括濃度為0.1毫克/公升的金離子、濃度為20毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例4的廢水包括濃度為0.01毫克/公升的金離子、濃度為20毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。而實驗例1、實驗例2、實驗例3以及實驗例4的反應條件皆為:硫脲石墨烯為2.0毫克、反應溫度為30℃、振盪速度為150 rpm、pH值為2、反應體積為50毫升、反應時間為96小時。In this embodiment, the wastewater is divided into experimental example 1, experimental example 2, and experimental example 3 according to the composition and content of the wastewater. Among them, the wastewater of Experimental Example 1 includes gold ions with a concentration of 10 mg/liter, copper ions with a concentration of 20 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 2 includes gold ions with a concentration of 1 mg/liter, copper ions with a concentration of 20 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 3 includes gold ions with a concentration of 0.1 mg/liter, copper ions with a concentration of 20 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 4 includes gold ions with a concentration of 0.01 mg/liter, copper ions with a concentration of 20 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The reaction conditions of Experimental Example 1, Experimental Example 2, Experimental Example 3, and Experimental Example 4 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50 ml, the reaction time is 96 hours.

由圖5B的結果可知,在實驗例1中,硫脲石墨烯對金離子的吸附效率為98.3±0.8%,但對銅離子、鉛離子及鋅離子皆不具有吸附效率。在實驗例3中,硫脲石墨烯對金離子的吸附效率為98.9±0.3%,對鉛離子的吸附效率約為1%至2%,但對銅離子及鋅離子皆不具有吸附效率。在實驗例4中,硫脲石墨烯對金離子的吸附效率為100%,但對銅離子、鉛離子及鋅離子皆不具有吸附效率。因此,硫脲石墨烯對金離子的最低可吸附濃度(最低吸附極限)為0.01毫克/公升。此外,當金離子為0.01毫克/公升至10毫克/公升時,硫脲石墨烯對金離子皆具有高選擇性以及98%以上的吸附效率。It can be seen from the result of FIG. 5B that in Experimental Example 1, the adsorption efficiency of thiourea graphene for gold ions is 98.3±0.8%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions. In Experimental Example 3, the adsorption efficiency of thiourea graphene for gold ions is 98.9±0.3%, and the adsorption efficiency for lead ions is about 1% to 2%, but it has no adsorption efficiency for copper ions and zinc ions. In Experimental Example 4, the adsorption efficiency of thiourea graphene for gold ions is 100%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions. Therefore, the lowest adsorbable concentration (lowest adsorption limit) of thiourea graphene for gold ions is 0.01 mg/L. In addition, when gold ions range from 0.01 mg/liter to 10 mg/liter, thiourea graphene has high selectivity for gold ions and an adsorption efficiency of over 98%.

實施例Example 77 :廢水中的銅離子濃度對硫脲石墨烯的吸附效率的影響:The influence of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene

在本實施例中,依據廢水的組成成份及其含量分為實驗例5、實驗例6、實驗例7以及實驗例8。其中,實驗例5的廢水包括濃度為10毫克/公升的金離子、濃度為100毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例6的廢水包括濃度為1毫克/公升的金離子、濃度為100毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例7的廢水包括濃度為0.1毫克/公升的金離子、濃度為100毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。實驗例8的廢水包括濃度為0.01毫克/公升的金離子、濃度為100毫克/公升的銅離子、濃度為20毫克/公升的鉛離子、濃度為20毫克/公升的鋅離子。而實驗例5、實驗例6、實驗例7以及實驗例8的反應條件皆為:硫脲石墨烯為2.0毫克、反應溫度為30℃、振盪速度為150 rpm、pH值為2、反應體積為50毫升、反應時間為96小時。In this embodiment, the wastewater is divided into experimental example 5, experimental example 6, experimental example 7, and experimental example 8 according to the composition and content of the wastewater. The wastewater of Experimental Example 5 includes gold ions with a concentration of 10 mg/liter, copper ions with a concentration of 100 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 6 includes gold ions with a concentration of 1 mg/liter, copper ions with a concentration of 100 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 7 includes gold ions with a concentration of 0.1 mg/liter, copper ions with a concentration of 100 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The wastewater of Experimental Example 8 includes gold ions with a concentration of 0.01 mg/liter, copper ions with a concentration of 100 mg/liter, lead ions with a concentration of 20 mg/liter, and zinc ions with a concentration of 20 mg/liter. The reaction conditions of Experimental Example 5, Experimental Example 6, Experimental Example 7 and Experimental Example 8 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50 ml, the reaction time is 96 hours.

由圖5C的結果可知,相較於圖5B的實驗例1,實驗例5中的硫脲石墨烯對金離子的吸附效率約略降低為95.4±0.5%,但對銅離子、鉛離子及鋅離子仍不具有吸附效率。此外,相較於圖5B的實驗例3,實驗例7中的硫脲石墨烯對金離子的吸附效率為98±1.5%,對鉛離子的吸附效率仍約為1%至2%,但對銅離子及鋅離子仍不具有吸附效率。相較於圖5B的實驗例4,實驗例8中的硫脲石墨烯對金離子的吸附效率為100%,對鉛離子的吸附效率約為5%,但對銅離子及鋅離子仍不具有吸附效率。因此,縱使提高廢水中的銅離子的濃度,硫脲石墨烯對金離子仍具有高選擇性以及95%至100%的吸附效率。It can be seen from the results in Figure 5C that compared to Experimental Example 1 in Figure 5B, the adsorption efficiency of thiourea graphene for gold ions in Experimental Example 5 is slightly reduced to 95.4±0.5%, but for copper ions, lead ions, and zinc ions. It still does not have adsorption efficiency. In addition, compared with Experimental Example 3 in Figure 5B, the thiourea graphene in Experimental Example 7 has an adsorption efficiency of 98±1.5% for gold ions, and the adsorption efficiency for lead ions is still about 1% to 2%, but the Copper and zinc ions still have no adsorption efficiency. Compared with Experimental Example 4 in Figure 5B, the thiourea graphene in Experimental Example 8 has an adsorption efficiency of 100% for gold ions and an adsorption efficiency of about 5% for lead ions, but it still has no effect on copper and zinc ions. Adsorption efficiency. Therefore, even if the concentration of copper ions in wastewater is increased, graphene thiourea still has high selectivity for gold ions and an adsorption efficiency of 95% to 100%.

綜上所述,在本發明提供的使用硫脲石墨烯之回收金的方法中,藉由硫脲石墨烯對於金離子的高選擇性,使得在利用硫脲石墨烯對廢水中的金離子進行吸附反應時,可具有較低的吸附極限、較佳的吸附效率以及較高的飽和吸附容量。To sum up, in the method for recovering gold using thiourea graphene provided by the present invention, the high selectivity of thiourea graphene for gold ions makes it possible to use thiourea graphene for gold ions in wastewater. During the adsorption reaction, it can have a lower adsorption limit, better adsorption efficiency and higher saturated adsorption capacity.

雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention. Anyone with ordinary knowledge in the technical field can make some changes and modifications without departing from the spirit and scope of the present invention. The scope of protection of the present invention shall be determined by the scope of the attached patent application.

S110、S120、S130、S140:步驟S110, S120, S130, S140: steps

圖1繪示為本發明一實施例的一種硫脲石墨烯之回收金的方法的流程圖。 圖2A為X光繞射的分析結果。 圖2B為掃瞄式電子顯微鏡的分析結果。 圖2C為穿透式電子顯微鏡的分析結果。 圖3A為不同的反應時間對硫脲石墨烯的吸附效率的影響。 圖3B為不同的反應的pH值對硫脲石墨烯的吸附效率的影響。 圖3C為不同劑量的硫脲石墨烯對其吸附效率的影響。 圖3D為不同濃度的硫代硫酸銨溶液對其脫附效率的影響。 圖4為硫脲石墨烯對金離子的等溫吸附曲線。 圖5A為氧化石墨烯及硫脲石墨烯分別對金離子、銅離子、鉛離子及鋅離子的吸附效率。 圖5B為硫脲石墨烯對廢水中的金離子、銅離子、鉛離子及鋅離子的選擇性以及最低吸附極限。 圖5C為廢水中的銅離子濃度對硫脲石墨烯的吸附效率的影響。 FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention. Figure 2A shows the analysis result of X-ray diffraction. Figure 2B shows the analysis result of the scanning electron microscope. Figure 2C shows the analysis result of a transmission electron microscope. Figure 3A shows the effect of different reaction times on the adsorption efficiency of thiourea graphene. Figure 3B shows the effect of different reaction pH values on the adsorption efficiency of thiourea graphene. Figure 3C shows the effect of different doses of thiourea graphene on its adsorption efficiency. Figure 3D shows the effect of different concentrations of ammonium thiosulfate solution on its desorption efficiency. Figure 4 shows the isothermal adsorption curve of thiourea graphene for gold ions. Figure 5A shows the adsorption efficiency of graphene oxide and graphene thiourea for gold ions, copper ions, lead ions, and zinc ions, respectively. Figure 5B shows the selectivity and lowest adsorption limit of thiourea graphene for gold ions, copper ions, lead ions and zinc ions in wastewater. Figure 5C shows the effect of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene.

S110、S120、S130、S140:步驟 S110, S120, S130, S140: steps

Claims (11)

一種使用硫脲石墨烯的方法,包括:提供一硫脲石墨烯,且該硫脲石墨烯的粒徑在0.25毫米至0.59毫米之間;將該硫脲石墨烯加入至一水溶液中,以進行一吸附反應,其中該水溶液至少包括一金離子,且該硫脲石墨烯會選擇性吸附該金離子,其中該吸附反應的反應條件包括:pH值為2至6,且該金離子的最低吸附極限為0.01毫克/公升;將吸附該金離子的該硫脲石墨烯與該水溶液分離;以及對吸附該金離子的該硫脲石墨烯進行一脫附反應,以得到含有該金離子的溶液。 A method of using thiourea graphene includes: providing a thiourea graphene, and the thiourea graphene has a particle size between 0.25 mm and 0.59 mm; adding the thiourea graphene to an aqueous solution to perform An adsorption reaction, wherein the aqueous solution includes at least one gold ion, and the thiourea graphene selectively adsorbs the gold ion, wherein the reaction conditions of the adsorption reaction include: a pH value of 2 to 6 and a minimum adsorption of the gold ion The limit is 0.01 mg/liter; the thiourea graphene adsorbing the gold ion is separated from the aqueous solution; and the thiourea graphene adsorbing the gold ion is subjected to a desorption reaction to obtain a solution containing the gold ion. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中該硫脲石墨烯的氮含量為2~4重量%,且硫含量為20~23重量%。 According to the method for using graphene thiourea as described in item 1 of the scope of patent application, the nitrogen content of graphene thiourea is 2 to 4% by weight, and the sulfur content is 20 to 23% by weight. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中該硫脲石墨烯為0.5毫克至2.0毫克。 The method for using graphene thiourea as described in item 1 of the scope of the patent application, wherein the graphene thiourea is 0.5 mg to 2.0 mg. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中該吸附反應的該反應條件更包括:反應時間為96小時以上。 According to the method for using graphene thiourea as described in item 1 of the scope of patent application, the reaction conditions of the adsorption reaction further include: the reaction time is more than 96 hours. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中該水溶液的該金離子的濃度為0.01毫克/公升至10毫克/公升。 In the method for using graphene thiourea as described in item 1 of the patent application, the concentration of the gold ion in the aqueous solution is 0.01 mg/liter to 10 mg/liter. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中該硫脲石墨烯對該金離子的吸附效率為95%至100%。 According to the method for using graphene thiourea as described in item 1 of the scope of patent application, the adsorption efficiency of graphene thiourea for gold ions is 95% to 100%. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中當該水溶液更包括銅離子、鉛離子、鋅離子或其組合時,該硫脲石墨烯對該鉛離子的吸附效率為1%至2%,且對銅離子及鋅離子的吸附效率為0%。 The method for using graphene thiourea as described in item 1 of the scope of patent application, wherein when the aqueous solution further includes copper ions, lead ions, zinc ions, or a combination thereof, the adsorption efficiency of the graphene thiourea for lead ions is 1% to 2%, and the adsorption efficiency of copper ions and zinc ions is 0%. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中每克該硫脲石墨烯對該金離子的飽和吸附容量為833.33毫克。 The method for using graphene thiourea as described in item 1 of the scope of patent application, wherein the saturated adsorption capacity of the graphene thiourea for gold ions per gram is 833.33 mg. 如申請專利範圍第1項所述的使用硫脲石墨烯的方法,其中對吸附該金離子的該硫脲石墨烯進行該脫附反應的步驟包括:將一脫附劑加入於吸附該金離子的該硫脲石墨烯中,以使該金離子從該硫脲石墨烯上脫附。 The method for using graphene thiourea as described in item 1 of the scope of the patent application, wherein the step of performing the desorption reaction on the graphene thiourea that adsorbs the gold ion includes: adding a desorbent to adsorb the gold ion In the thiourea graphene, the gold ions are desorbed from the thiourea graphene. 如申請專利範圍第9項所述的使用硫脲石墨烯的方法,其中該金離子的脫附效率為93%至96%。 According to the method for using graphene thiourea as described in item 9 of the scope of patent application, the desorption efficiency of the gold ion is 93% to 96%. 一種如申請專利範圍第1項至第10項中任一項所述的使用硫脲石墨烯的方法的用途,其係用於從廢水中回收金。 A use of the method for using thiourea graphene as described in any one of the first to the tenth items of the scope of patent application, which is used to recover gold from wastewater.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW201412646A (en) * 2012-09-21 2014-04-01 Nat Univ Kaohsiung Noble metal adsorption material and noble metal recycling method using the same
CN105771903A (en) * 2016-03-07 2016-07-20 河南师范大学 Preparation method of thiourea modified ZIF-8 material for selectively adsorbing gold
CN108380177A (en) * 2018-03-09 2018-08-10 浙江农林大学 A kind of preparation method of magnetism modified graphene oxide hydrogel
CN108439372A (en) * 2018-02-07 2018-08-24 山东大学 Sulfur and nitrogen co-doped graphene-based aeroge of one kind and preparation method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW201412646A (en) * 2012-09-21 2014-04-01 Nat Univ Kaohsiung Noble metal adsorption material and noble metal recycling method using the same
CN105771903A (en) * 2016-03-07 2016-07-20 河南师范大学 Preparation method of thiourea modified ZIF-8 material for selectively adsorbing gold
CN108439372A (en) * 2018-02-07 2018-08-24 山东大学 Sulfur and nitrogen co-doped graphene-based aeroge of one kind and preparation method thereof
CN108380177A (en) * 2018-03-09 2018-08-10 浙江农林大学 A kind of preparation method of magnetism modified graphene oxide hydrogel

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