TWI446960B - A Method for Making Precious Metal Adsorbents - Google Patents

A Method for Making Precious Metal Adsorbents Download PDF

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TWI446960B
TWI446960B TW100128285A TW100128285A TWI446960B TW I446960 B TWI446960 B TW I446960B TW 100128285 A TW100128285 A TW 100128285A TW 100128285 A TW100128285 A TW 100128285A TW I446960 B TWI446960 B TW I446960B
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monomer
precious metal
metal adsorbent
adsorbent according
composition
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TW201306938A (en
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Yen Chung Chen
Chih Kai Chang
Hsiou Jeng Shy
Ching Yu Tso
Jen Bin Won
Ming Der Ger
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Nat Inst Chung Shan Science & Technology
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Description

一種貴重金屬吸附劑的製作方法 Method for preparing precious metal adsorbent

本發明係揭露一種貴重金屬吸附劑之製作方法,特別是應用於吸附劑、塗料、乳液樹脂、黏合劑、聚合物混凝土及紡織漿料等原料用途。 The invention discloses a method for preparing a precious metal adsorbent, in particular to a raw material used for an adsorbent, a coating, an emulsion resin, a binder, a polymer concrete and a textile slurry.

習知金屬礦物原料缺乏,在全球資訊與消費性電子產品不斷推出下,其產品生命週期縮短及快速汰換,造成了大量的電子廢棄物,該廢棄物中不少含有多種基本金屬及貴重金屬,重金屬廢棄物來源廣泛,涉及之行業包含礦山、冶金、機械製造、化工、電子及儀表等,且重金屬通常具有急性或慢性毒性,有時會以更複雜之方式毒害生物體,以致影響整個食物鏈,隨著對重金屬毒物學的深入研究及檢測技術的發展,重金屬廢棄物的處理處置標準趨向嚴格,除了一部份可回收利用外,其餘大部分,都需進行穩定化處理以達到無害化之目的。 The lack of known metal mineral raw materials, the continuous shortening of the product life cycle and the rapid replacement of global information and consumer electronic products, resulting in a large amount of electronic waste, many of which contain a variety of basic metals and precious metals Heavy metal waste comes from a wide range of industries, including mining, metallurgy, machinery manufacturing, chemicals, electronics and instrumentation. Heavy metals often have acute or chronic toxicity, sometimes poisoning organisms in more complex ways, affecting the entire food chain. With the in-depth study of heavy metal toxicology and the development of detection technology, the treatment and disposal standards for heavy metal waste tend to be strict. Except for some parts that can be recycled, most of them need to be stabilized to achieve harmlessness. purpose.

近幾十年來,合成性質特殊的高分子複合微球備受關注,是一種新穎的高分子材料,其中由甲基丙烯酸甲酯(MMA)單體聚合成之聚甲基丙烯酸甲酯(PMMA)高分子微球是一種重要的有機透明結構材料,它具有透明度高、耐候性好、物理機械性能比較均勻、加工性能優異等優點。然而它尚存在耐熱性較低、金屬吸附率偏低、機械強度還不夠及缺乏功能性基團等缺點;當使用高分子微球經過共聚或表面 改性後,其表面可引入不同的功能基團(如-COOH、-NH2、-OH、-SO3H、-CH3Cl等),從而使材料獲得了新的性能,帶有功能基團的親水性聚合物,易分佈於微球表面,從而使其表面功能化,其中以含羧基的高分子微球的應用範圍最廣,由於羧酸分子極易與各種分子反應,因而對表面帶有羧酸功能基的高分子微球的合成倍受關注。國內外已有眾多學者運用不同的聚合方法合成了表面帶羧酸基團的高分子微球,可應用於吸附蛋白質當作疫苗,骨骼黏合應用、水處理以及工業廢水的處理等,有著重要的應用前景。故以高分子微球作為吸附劑,其主要優點為製作步驟簡易及成本較低,但其金屬吸附率、吸附速度及金屬選擇性仍有待改進。 In recent decades, polymer composite microspheres with special synthetic properties have attracted much attention. It is a novel polymer material in which polymethyl methacrylate (PMMA) is polymerized from methyl methacrylate (MMA) monomer. Polymer microspheres are an important organic transparent structural material, which has the advantages of high transparency, good weather resistance, uniform physical and mechanical properties, and excellent processing performance. However, it has the disadvantages of low heat resistance, low metal adsorption rate, insufficient mechanical strength and lack of functional groups. When polymer microspheres are copolymerized or surface modified, different functional groups can be introduced on the surface. Groups (such as -COOH, -NH 2 , -OH, -SO 3 H, -CH 3 Cl, etc.), so that the material obtains new properties, hydrophilic polymers with functional groups, easy to distribute in microspheres Surface, thereby functionalizing its surface, wherein the carboxyl group-containing polymer microspheres have the widest application range, and since the carboxylic acid molecules are easily reacted with various molecules, the polymer microspheres having a carboxylic acid functional group on the surface are Synthesis has received much attention. Many scholars at home and abroad have used different polymerization methods to synthesize polymer microspheres with carboxylic acid groups on the surface. They can be applied to adsorbed proteins as vaccines, bone bonding applications, water treatment and industrial wastewater treatment. Application prospects. Therefore, the main advantage of the polymer microspheres as the adsorbent is that the production process is simple and the cost is low, but the metal adsorption rate, adsorption speed and metal selectivity still need to be improved.

2005年Cox等人利用活性碳,研究其吸附貴金屬之速率依次為Au(Ⅲ)>Pd(Ⅱ)>Ag(I)>Pt(Ⅱ)Pt(Ⅳ)。研究顯示活性碳比表面積大,有利於貴金屬之吸附,但是選擇性差,而且再生困難為其主要缺點。2002年Say等人將該粒子係為poly(HEMA-EGDMA)配合2-methacrylamidohistidine(MAH)螯合劑進行改質,其對貴金屬離子有很好的吸附效果。U.S.Patent NO.5,115,036和U.S.Patent NO.5,064,879以乙烯與丙烯酸胺基烷酯(aminoalkyl acrylate)之共聚物,其官能基帶陰電性用於螯合金屬離子的廢水處理方法。此方法的反應時間相當長(3~16小時不等),且反應完後必須將金屬離子脫附下來,對於儀器設備成本來說又是一大考驗。 In 2005, Cox et al. used activated carbon to study the rate of adsorption of noble metals by Au(III)>Pd(II)>Ag(I)>Pt(II). Pt(IV). Studies have shown that activated carbon has a large specific surface area, which is favorable for the adsorption of precious metals, but the selectivity is poor, and the difficulty of regeneration is its main disadvantage. In 2002, Say et al. modified the particle system with poly(HEMA-EGDMA) and 2-methacrylamidohistidine (MAH) chelating agent, which has a good adsorption effect on noble metal ions. US Patent No. 5,115,036 and US Patent No. 5,064,879 are copolymers of ethylene and an aminoalkyl acrylate, the functional group of which is electrically anionic for the treatment of metal ions. The reaction time of this method is quite long (ranging from 3 to 16 hours), and the metal ions must be desorbed after the reaction, which is a big test for the cost of the equipment.

故本發明即揭露一種新穎貴重金屬吸附劑的製作方法,該方法可達到簡化製程、縮短反應時間、降低成本及高經濟效益之目的,以解決上述問題。 Therefore, the present invention discloses a method for preparing a novel precious metal adsorbent, which can solve the above problems by simplifying the process, shortening the reaction time, reducing the cost and high economic benefit.

鑒於上述習知技術之缺點,本發明主要目的在於提供一種貴重金屬吸附劑的製作方法,利用該方法製備之貴重金屬吸附劑可達到選擇性吸附、反應時間短及具高經濟效率之目的。 In view of the above disadvantages of the prior art, the main object of the present invention is to provide a method for preparing a precious metal adsorbent, and the precious metal adsorbent prepared by the method can achieve selective adsorption, short reaction time and high economic efficiency.

為了達到上述目的本發明提供一種貴重金屬吸附劑的製作方法,其步驟係為(A)提供單體1之組成及單體2之組成;(B)將單體2之組成加入單體1之組成;(C)進行微波反應得貴重金屬吸附劑粒子。 In order to achieve the above object, the present invention provides a method for producing a precious metal adsorbent, which comprises the steps of: (A) providing the composition of the monomer 1 and the composition of the monomer 2; (B) adding the composition of the monomer 2 to the monomer 1. Composition; (C) performing a microwave reaction to obtain precious metal adsorbent particles.

步驟(A)中單體1之組成係包括單體1及溶劑,單體2之組成係包括單體2、起始劑及陽離子分散劑(MTC),其中單體1及單體2係為甲基丙烯酸甲酯、苯乙烯、醋酸乙烯酯、丙烯酸、甲基丙烯酸、三氟甲基丙烯酸、亞甲基丁二酸、乙烯機苯甲酸等可聚合之有機單體,且單體1及單體2係可為同一種化合物,本發明之較佳實施例單體1係甲基丙烯酸甲酯及單體2係丙烯酸。溶劑係為含微量鹽類的水溶液,該鹽類係為氯化鈉(NaCl)及氯化銨(NH4Cl)等其中之一,該水溶液之水係為純水。起始劑係為偶氮二異丁腈(azobisisobutyronitrile,簡稱AIBN)、過氧化月桂醯(lauroyl peroxide,簡稱LPO)、 過硫酸銨(ammonium persulfate,簡稱APS)、過硫酸鉀(potassium persulphate,簡稱KPS)等。陽離子分散劑係為甲基丙烯醯氧甲基三甲基氯化銨(2-(methacryloyloxy)methyl-trimethylammonium chloride)、甲基丙烯醯氧乙基三甲基氯化銨(2-(methacryloyloxy)ethyl-trimethylammonium chloride)、3-(甲基丙烯醯氧)丙基三甲氧基矽烷(3-methacryloxy-propyl-trimethoxysilane)及鹽酸或硫酸混合液、甲基丙烯醯氧甲基三甲基氯化銨以及甲基丙烯醯氧乙基三甲基氯化銨混合液等。其中,步驟(C)中微波反應使用之反應器係包含一冷卻裝置,該裝置可用於確認在反應的期間都是在進行微波加熱反應。 The composition of the monomer 1 in the step (A) includes the monomer 1 and the solvent, and the composition of the monomer 2 includes the monomer 2, the initiator and the cationic dispersant (MTC), wherein the monomer 1 and the monomer 2 are Polymerizable organic monomer such as methyl methacrylate, styrene, vinyl acetate, acrylic acid, methacrylic acid, trifluoromethyl methacrylate, methylene succinic acid, ethylene benzoic acid, and monomer 1 and single The bulk 2 may be the same compound. In the preferred embodiment of the invention, monomer 1 is methyl methacrylate and monomer 2 is acrylic acid. The solvent is an aqueous solution containing a trace amount of a salt, and the salt is one of sodium chloride (NaCl) and ammonium chloride (NH 4 Cl), and the aqueous solution is pure water. The initiator is azobisisobutyronitrile (AIBN), lauroyl peroxide (LPO), ammonium persulfate (APS), potassium persulphate (KPS). )Wait. The cationic dispersant is 2-(methacryloyloxymethyl)methyl-trimethylammonium chloride or 2-propenyloxyethyltrimethylammonium chloride (2-(methacryloyloxy)ethyl) -trimethylammonium chloride), 3-methacryloxy-propyl-trimethoxysilane, and a mixture of hydrochloric acid or sulfuric acid, methacryloyloxymethyltrimethylammonium chloride, and A mixture of methacrylic acid oxiranyl trimethylammonium chloride or the like. Wherein, the reactor used in the microwave reaction in the step (C) comprises a cooling device which can be used to confirm that the microwave heating reaction is carried out during the reaction.

為了取得貴重金屬吸附劑粒子,本發明之實施例中提出另一方案,提供一種貴重金屬吸附劑之製作方法,其步驟係包括(A)提供單體1之組成及單體2之組成;(B)將單體2之組成加入單體1之組成;(C)進行微波反應得貴重金屬吸附劑粒子;(D)係將步驟(C)中之該溶液進行離心程序;(E)該粒子進行過濾及洗滌程序;(F)過濾出之粒子進行乾燥程序。藉此,透過本發明以達到高效率及簡化製程之目的,且本發明實施例中製備之貴重金屬吸附劑具有粒徑分佈窄、選擇性佳及吸附量高等優點。 In order to obtain the precious metal adsorbent particles, another embodiment of the present invention provides a method for preparing a precious metal adsorbent, the steps of which include (A) providing the composition of the monomer 1 and the composition of the monomer 2; B) adding the composition of the monomer 2 to the composition of the monomer 1; (C) performing a microwave reaction to obtain the precious metal adsorbent particles; (D) performing the centrifugation procedure of the solution in the step (C); (E) the particle The filtration and washing procedures are carried out; (F) the filtered particles are subjected to a drying procedure. Thereby, the invention achieves high efficiency and simplifies the process, and the precious metal adsorbent prepared in the embodiment of the invention has the advantages of narrow particle size distribution, good selectivity and high adsorption amount.

以上之概述與接下來的詳細說明及附圖,皆是為了能進一步說明本發明達到預定目的所採取的方式、手段及功效。而有關本發明的其它目的及優點,將在後續的說明及圖示中 加以闡述。 The above summary, the following detailed description and the accompanying drawings are intended to further illustrate the manner, the Other objects and advantages of the present invention will be described in the following description and illustration. Explain it.

以下係藉由特定的具體實例說明本發明之實施方式,熟悉此技藝之人士可由本說明書所揭示之內容輕易地瞭解本發明之其它優點與功效。 The embodiments of the present invention are described below by way of specific examples, and those skilled in the art can readily appreciate the other advantages and advantages of the present invention.

請參閱第1圖所示,本發明係以合成一種貴重金屬吸附劑,其步驟係包括:步驟(A):提供單體1之組成及單體2之組成(11),其中單體1之組成係包括單體1及溶劑,單體2之組成係包括單體2、起始劑及陽離子分散劑(MTC),於本實施例中單體1及單體2係為甲基丙烯酸甲酯、苯乙烯、醋酸乙烯酯、丙烯酸、甲基丙烯酸、三氟甲基丙烯酸、亞甲基丁二酸、乙烯基苯甲酸等,且單體1及單體2係可為同一種化合物;步驟(B):將單體2之組成加入單體1之組成(12),單體2須依一定比例且均勻攪拌下加入單體1;步驟(C):進行微波反應得貴重金屬吸附劑粒子(13),微波反應之條件如下列所示:反應時間可為5至120分鐘,功率可為30W至300W,反應溫度可為60℃至85℃。 Referring to Figure 1, the present invention is to synthesize a precious metal adsorbent, the steps of which include: step (A): providing the composition of monomer 1 and the composition of monomer 2 (11), wherein monomer 1 The composition includes the monomer 1 and the solvent, and the composition of the monomer 2 includes the monomer 2, the initiator and the cationic dispersant (MTC). In the present embodiment, the monomer 1 and the monomer 2 are methyl methacrylate. , styrene, vinyl acetate, acrylic acid, methacrylic acid, trifluoromethacrylic acid, methylene succinic acid, vinyl benzoic acid, etc., and monomer 1 and monomer 2 can be the same compound; B): adding the composition of the monomer 2 to the composition (12) of the monomer 1, the monomer 2 is added to the monomer 1 under a certain ratio and uniform stirring; and the step (C): performing the microwave reaction to obtain the precious metal adsorbent particles ( 13) The conditions of the microwave reaction are as follows: the reaction time may be 5 to 120 minutes, the power may be 30 W to 300 W, and the reaction temperature may be 60 to 85 °C.

請參閱第2圖所示,係本發明一種貴重金屬吸附劑另一種製程示意圖,其步驟係包括:步驟(A)提供單體1之組成及單體2之組成(21);步驟(B)將單體2之組成加入單體1之組成(22);步驟(C)進行微波反應得貴重金屬吸附劑粒子(23);步驟(D)係將步驟(C)中之該溶液進行離心程序(24);步驟(E)該粒子進行過濾及洗滌程序(25);步驟(F)過濾出之粒子進行乾燥程序(26)。該粒子具有比表面積大、吸附速度快、 具有選擇性吸附、流動性優異等特性,為更加說明本發明,以下列實施例說明之。 Please refer to FIG. 2, which is a schematic diagram of another process of a precious metal adsorbent according to the present invention. The steps include the steps of: (A) providing the composition of the monomer 1 and the composition of the monomer 2 (21); and the step (B) The composition of the monomer 2 is added to the composition of the monomer 1 (22); the step (C) is subjected to microwave reaction to obtain the precious metal adsorbent particles (23); and the step (D) is the centrifugation of the solution in the step (C). (24); Step (E) The particles are subjected to a filtration and washing procedure (25); and the particles (F) filtered are subjected to a drying procedure (26). The particles have a large specific surface area and a fast adsorption speed. The characteristics of selective adsorption, excellent fluidity, and the like are described in the following examples in order to further illustrate the present invention.

實施例一: Embodiment 1:

首先將5克甲基丙烯酸甲酯單體(MMA monomer)與0.1克起始劑偶氮二異丁腈(azobisisobutyronitrile,AIBN)混合形成有機相。介質組成為40克甲醇、10克純水及0.1克陽離子分散劑(MTC)加入介質中,然後加入一定量丙烯酸(acrylic acid,AA),攪拌20分鐘使溶液混成均勻相。微波反應條件及參數如下:使用機型為CEM公司出產的Discover微波反應器。反應前的甲基丙烯酸甲酯溶液為澄清透明的水溶液,將此溶液倒入100mL圓底燒瓶,置入微波反應器中進行微波反應。將其微波反應器的反應模式設定為標準模式,微波瓦數為150W,反應溫度為75℃,每一樣品設定添加丙烯酸量分別為0.1、0.2、0.3、0.4、0.5克重,啟動空氣冷卻(Power MAX),反應結束後微波反應器會藉由空氣幫浦的空氣將反應物冷卻至50℃,即可獲得聚甲基丙烯酸甲酯交聯丙烯酸分散溶液,請參閱表一,經粒徑分析儀分析,不同的丙烯酸添加量對聚甲基丙烯酸甲酯交聯丙烯酸粒徑的影響。取少量樣品以粒徑分析儀及SEM進行量測,空氣冷卻(Power MAX)的功能為可藉由冷卻氣體持續地冷卻反應容器,並同時進行微波照射。由於傳統的微波反應器為在溫度達到設定溫度時,自動將微波功率調降或完全關閉,因此傳統的熱化學作用會取代微波加熱化學,然而若採用空氣冷卻系統功 能,在反應中同時不斷導入高壓空氣予以冷卻反應物,如此可確認在反應的期間都是在進行微波加熱反應。其中微波反應時間可為5至120分鐘,微波功率可為30W至300W,微波反應溫度可為60至85℃。 First, 5 g of methyl methacrylate monomer (MMA monomer) was mixed with 0.1 g of the initiator azobisisobutyronitrile (AIBN) to form an organic phase. The medium composition was 40 g of methanol, 10 g of pure water and 0.1 g of cationic dispersant (MTC) were added to the medium, then a certain amount of acrylic acid (AA) was added, and the mixture was stirred for 20 minutes to mix the solution into a homogeneous phase. The microwave reaction conditions and parameters are as follows: The model is a Discover microwave reactor produced by CEM. The methyl methacrylate solution before the reaction was a clear and transparent aqueous solution, and the solution was poured into a 100 mL round bottom flask and placed in a microwave reactor for microwave reaction. The reaction mode of the microwave reactor was set to the standard mode, the microwave wattage was 150 W, the reaction temperature was 75 ° C, and the amount of acrylic acid added for each sample was 0.1, 0.2, 0.3, 0.4, 0.5 gram, respectively, and the air cooling was started ( Power MAX), after the reaction is completed, the microwave reactor will cool the reactants to 50 ° C by the air of the air pump to obtain a polymethyl methacrylate crosslinked acrylic acid dispersion solution. Please refer to Table 1 for particle size analysis. The instrument analyzed the effect of different amounts of acrylic acid on the particle size of polymethyl methacrylate crosslinked acrylic acid. A small amount of sample was measured by a particle size analyzer and SEM. The function of air cooling (Power MAX) was to continuously cool the reaction vessel by cooling gas and simultaneously irradiate the microwave. Since the conventional microwave reactor automatically reduces or completely shuts down the microwave power when the temperature reaches the set temperature, the conventional thermochemical action will replace the microwave heating chemistry, but if the air cooling system is used, In the reaction, high-pressure air was continuously introduced to cool the reactants, and it was confirmed that the microwave heating reaction was performed during the reaction. The microwave reaction time may be 5 to 120 minutes, the microwave power may be 30W to 300W, and the microwave reaction temperature may be 60 to 85 °C.

微波反應係另添加0.1克丙烯酸(AA)時,微球中間粒徑為3.67μm,丙烯酸(AA)添加量為0.5克時,粒徑增加至6.01μm,與之前無添加丙烯酸(AA)的聚合進行比較,發現添加丙烯酸(AA)可大幅提高粒子粒徑。 When the microwave reaction system is further added with 0.1 g of acrylic acid (AA), the intermediate particle diameter of the microspheres is 3.67 μm, and when the amount of acrylic acid (AA) is 0.5 g, the particle diameter is increased to 6.01 μm, and the polymerization with no prior acrylic acid (AA) is added. Comparing, it was found that the addition of acrylic acid (AA) can greatly increase the particle size.

於此實施例中,欲驗證經微波反應後粒子的形狀,將製得之聚甲基丙烯酸甲酯交聯丙烯酸(Poly(MMA-MTC-AA))更進一步提出下列步驟:將該聚甲基丙烯酸甲酯交聯丙烯酸溶液進行離心洗滌;以及取出該聚甲基丙烯酸甲酯交聯丙烯酸溶 液中之一溶質並對該溶質進行乾燥處理,以得到該聚甲基丙烯酸甲酯交聯丙烯酸(Poly(MMA-MTC-AA))粒子,其中乾燥溫度可為50至90℃,乾燥時間可為2至24小時,形成乾燥的聚甲基丙烯酸甲酯交聯丙烯酸(Poly(MMA-MTC-AA))粒子。第3圖係以添加丙烯酸(AA)0.1g較佳實施例製得之(Poly(MMA-MTC-AA))粒子掃瞄式電子顯微鏡(SEM)分析圖,其中聚甲基丙烯酸甲酯奈米粒子形成粒徑可介於3微米至7微米(31)。 In this embodiment, in order to verify the shape of the particles after the microwave reaction, the obtained polymethyl methacrylate crosslinked acrylic acid (Poly (MMA-MTC-AA)) further proposes the following steps: the polymethyl group Methyl acrylate cross-linked acrylic acid solution for centrifugal washing; and removing the polymethyl methacrylate cross-linked acrylic acid solution One of the solute in the liquid and drying the solute to obtain the polymethyl methacrylate crosslinked acrylic acid (Poly (MMA-MTC-AA)) particles, wherein the drying temperature can be 50 to 90 ° C, the drying time can be Dry polymethyl methacrylate crosslinked acrylic acid (Poly (MMA-MTC-AA)) particles were formed for 2 to 24 hours. Figure 3 is a scanning electron microscope (SEM) analysis of a Poly(MMA-MTC-AA) particle prepared by adding 0.1 g of acrylic acid (AA). The polymethyl methacrylate nanometer. The particle formation particle size can range from 3 microns to 7 microns (31).

實施例二: Embodiment 2:

一種貴重金屬吸附劑的製備方法,所合成的聚甲基丙烯酸甲酯交聯丙烯酸(Poly(MMA-MTC-AA))粒子的應用,貴重離子溶液的吸附方法,針對重金屬離子溶液與聚甲基丙烯酸甲酯交聯丙烯酸粒子進行吸附。其中一種含貴重金屬溶液的處理方法,包含表面鍵結有羧基官能基的聚甲基丙烯酸甲酯交聯丙烯酸粒子(Poly(MMA-MTC-AA))與含有貴重金屬離子的溶液溫度介於室溫至95℃,使該貴重金屬離子被還原成元素態且附著於粒子的表面。其中貴金屬離子吸附元素可為Au(Ⅲ)、Pd(Ⅱ)、Ag(I)、Pt(Ⅱ)、Pt(Ⅳ)、銅(Ⅱ)及銦(Ⅱ)等。 A method for preparing a precious metal adsorbent, a polymethyl methacrylate crosslinked acrylic acid (Poly(MMA-MTC-AA)) particle, a noble ion solution adsorption method, and a heavy metal ion solution and a polymethyl group The methyl acrylate crosslinked acrylic particles are adsorbed. One of the treatment methods containing a precious metal solution, comprising a polymethyl methacrylate crosslinked acrylic particle (Poly(MMA-MTC-AA)) having a carboxyl functional group bonded to the surface thereof and a solution containing a precious metal ion having a temperature in the chamber At a temperature of 95 ° C, the precious metal ions are reduced to an elemental state and attached to the surface of the particles. The noble metal ion adsorbing elements may be Au (III), Pd (II), Ag (I), Pt (II), Pt (IV), copper (II), and indium (II).

首先使用聚甲基丙烯酸甲酯(PMMA)作為貴金屬吸附用途,選擇傳統PMMA、PMMA-MTC(以MTC作分散劑)、Poly(MMA-MTC-AA)(以MTC作分散劑)等三種樣品為對象,進行一系列鈀吸附比較,同時與傳統製法以聚乙烯基吡咯烷酮 (PVP)為分散劑所得之聚甲基丙烯酸甲酯(PMMA)。係取10ml含Poly(MMA-MTC-AA)的粒子溶液,加入500ppm鈀離子溶液,在室溫下攪拌30分鐘,溶液會由白色轉變成黑色,將已吸附鈀之高分子微球溶液經過抽氣過濾,以得到澄清濾液,並進一步利用ICP分析濾液中的鈀離子濃度。由表二可知,PMMA、Poly(MMA-MTC)、Poly(MMA-MTC-AA)等三種高分子微球吸附鈀後,濾液中殘留鈀離子濃度依序為257ppm、66-75ppm,小於6ppm。 First, use polymethyl methacrylate (PMMA) as a precious metal adsorption application, and select three kinds of samples, such as traditional PMMA, PMMA-MTC (using MTC as dispersant), and Poly (MMA-MTC-AA) (using MTC as dispersant). Object, a series of palladium adsorption comparisons, and the traditional method of polyvinylpyrrolidone (PVP) is a polymethyl methacrylate (PMMA) obtained as a dispersant. Take 10ml of the solution containing Poly (MMA-MTC-AA), add 500ppm palladium ion solution, stir at room temperature for 30 minutes, the solution will change from white to black, and the polymer microsphere solution with adsorbed palladium will be pumped. Gas filtration was carried out to obtain a clear filtrate, and the palladium ion concentration in the filtrate was further analyzed by ICP. It can be seen from Table 2 that after the adsorption of palladium by three polymer microspheres such as PMMA, Poly (MMA-MTC), and Poly (MMA-MTC-AA), the residual palladium ion concentration in the filtrate is 257 ppm, 66-75 ppm, and less than 6 ppm.

由上可知,Poly(MMA-MTC-AA)高分子微球的吸附效果最佳,研究顯示微波反應系添加丙烯酸(AA),高分子微球表面含有羧基官能基會與鈀產生吸附,而且羧基官能基在溫度較高時,可加速貴金屬離子還原吸附於微球表面,使貴金屬吸附量提升。 It can be seen from the above that Poly (MMA-MTC-AA) polymer microspheres have the best adsorption effect. Studies have shown that the microwave reaction system is added with acrylic acid (AA), and the surface of the polymer microspheres contains carboxyl functional groups which will adsorb with palladium and carboxyl groups. When the functional group is at a higher temperature, the noble metal ions can be accelerated and adsorbed on the surface of the microspheres, so that the adsorption amount of the precious metal is increased.

綜觀來說,本發明提供一種貴重金屬吸附劑的製備方法,所合成的聚甲基丙烯酸甲酯交聯丙烯酸(Poly(MMA-MTC-AA))粒子,它具有提供一種粒徑分佈窄、反應快速、成本低、製程容易、選擇性佳及吸附量高等優點。 In summary, the present invention provides a method for preparing a precious metal adsorbent, which comprises a polymethyl methacrylate crosslinked acrylic acid (Poly (MMA-MTC-AA)) particle, which has a narrow particle size distribution and a reaction. Fast, low cost, easy process, good selectivity and high adsorption capacity.

上述之實施例僅為例示性說明本發明之特點及其功效,而非用於限制本發明之實質技術內容的範圍。任何熟悉此技藝之人士均可在不違背本發明之精神及範疇下,對上述實施例進行修飾與變化。因此,本發明之權利保護範圍,應如後述之申請專利範圍所列。 The above-described embodiments are merely illustrative of the features and functions of the present invention, and are not intended to limit the scope of the technical scope of the present invention. Modifications and variations of the above-described embodiments can be made by those skilled in the art without departing from the spirit and scope of the invention. Therefore, the scope of protection of the present invention should be as set forth in the scope of the claims described below.

11~13‧‧‧步驟 11~13‧‧‧Steps

21~26‧‧‧步驟 21~26‧‧‧Steps

31‧‧‧吸附劑粒子 31‧‧‧ adsorbent particles

第1圖係為本發明貴重金屬吸附劑之製程示意圖。 Figure 1 is a schematic view showing the process of the precious metal adsorbent of the present invention.

第2圖係為本發明貴重金屬吸附劑之另一製程示意圖。 Figure 2 is a schematic view of another process of the precious metal adsorbent of the present invention.

第3圖係為本發明實施例一之掃瞄式電子顯微鏡分析圖。 Fig. 3 is a scanning electron microscope analysis diagram of the first embodiment of the present invention.

11~13‧‧‧步驟 11~13‧‧‧Steps

Claims (12)

一種貴重金屬吸附劑的製作方法,其步驟包括:(A)提供單體1之組成及單體2之組成;(B)將單體2之組成加入單體1之組成;(C)進行微波反應得貴重金屬吸附劑粒子。 A method for preparing a precious metal adsorbent, the steps comprising: (A) providing the composition of the monomer 1 and the composition of the monomer 2; (B) adding the composition of the monomer 2 to the composition of the monomer 1; (C) performing microwave The precious metal adsorbent particles are reacted. 如申請專利範圍第1項所述之一種貴重金屬吸附劑的製作方法,其中,單體1之組成係包括單體1及溶劑。 A method for producing a precious metal adsorbent according to claim 1, wherein the monomer 1 comprises a monomer 1 and a solvent. 如申請專利範圍第1項所述之一種貴重金屬吸附劑的製作方法,其中,單體2之組成係包括單體2、起始劑及陽離子分散劑。 The method for producing a precious metal adsorbent according to claim 1, wherein the composition of the monomer 2 comprises a monomer 2, an initiator, and a cationic dispersant. 如申請專利範圍第1項所述之一種貴重金屬吸附劑的製作方法,其中,單體1及單體2係為甲基丙烯酸甲酯、苯乙烯、醋酸乙烯酯、丙烯酸、甲基丙烯酸、三氟甲基丙烯酸、亞甲基丁二酸、乙烯基苯甲酸等可聚合之有機單體,且單體1及單體2係可為同一種化合物。 The method for preparing a precious metal adsorbent according to claim 1, wherein the monomer 1 and the monomer 2 are methyl methacrylate, styrene, vinyl acetate, acrylic acid, methacrylic acid, and the like. A polymerizable organic monomer such as fluoromethacrylic acid, methylene succinic acid or vinyl benzoic acid, and the monomer 1 and the monomer 2 may be the same compound. 如申請專利範圍第2項所述之一種貴重金屬吸附劑的製作方法,其中,溶劑係為含微量鹽類的水溶液,該鹽類係為氯化鈉(NaCl)及氯化銨(NH4Cl)等其中之一;該水溶液之水係為純水。 The method for producing a precious metal adsorbent according to claim 2, wherein the solvent is an aqueous solution containing a trace amount of a salt, and the salt is sodium chloride (NaCl) and ammonium chloride (NH 4 Cl). And one of them; the aqueous solution of the aqueous solution is pure water. 如申請專利範圍第5項所述之一種貴重金屬吸附劑的製作方法,其中,該溶劑中鹽類對純水之重量百分濃度為0.01%至1%。 The method for producing a precious metal adsorbent according to claim 5, wherein the concentration of the salt in the solvent to the pure water is 0.01% to 1% by weight. 如申請專利範圍第3項所述之一種貴重金屬吸附劑的製作方法,其中,起始劑係為偶氮二異丁腈(azobisisobutyronitrile,簡稱AIBN)、過氧化月桂醯(lauroyl peroxide,簡稱LPO)、過硫酸銨(ammonium persulfate,簡稱APS)、過硫酸鉀(potassium persulphate,簡稱KPS)等其中之一。 The method for preparing a precious metal adsorbent according to claim 3, wherein the initiator is azobisisobutyronitrile (AIBN) and lauroyl peroxide (LPO). , one of ammonium persulfate (APS) and potassium persulphate (KPS). 如申請專利範圍第3項所述之一種貴重金屬吸附劑的製作方法,其中,陽離子分散劑係為甲基丙烯醯氧甲基三甲基氯化銨(2-(methacryloyloxy)methyl-trimethylammonium chloride)、甲基丙烯醯氧乙基三甲基氯化銨(2-(methacryloyloxy)ethyl-trimethylammonium chloride)、3-(甲基丙烯醯氧)丙基三甲氧基矽烷(3-methacryloxy-propyl-trimethoxysilane)及鹽酸或硫酸混合液、甲基丙烯醯氧甲基三甲基氯化銨以及甲基丙烯醯氧乙基三甲基氯化銨混合液等其中之一。 The method for producing a precious metal adsorbent according to claim 3, wherein the cationic dispersant is 2-(methacryloyloxymethyl)methyl-trimethylammonium chloride. , 2-(methacryloyloxy)ethyl-trimethylammonium chloride, 3-methacryloxy-propyl-trimethoxysilane And one of a mixture of hydrochloric acid or sulfuric acid, a mixture of methacryloyloxymethyltrimethylammonium chloride, and a mixture of methacryloyloxyethyltrimethylammonium chloride. 如申請專利範圍第1項所述之一種貴重金屬吸附劑的製作方法,其中,微波反應之條件如下列所示:反應時間可為5至120分鐘,功率可為30W至300W,反應溫度可為60至85℃。 The method for preparing a precious metal adsorbent according to claim 1, wherein the microwave reaction conditions are as follows: the reaction time may be 5 to 120 minutes, the power may be 30 W to 300 W, and the reaction temperature may be 60 to 85 ° C. 如申請專利範圍第9項所述之一種貴重金屬吸附劑的製作方法,其中,微波反應使用之反應器係包含一冷卻裝置。 The method for producing a precious metal adsorbent according to claim 9, wherein the reactor used for the microwave reaction comprises a cooling device. 如申請專利範圍第1項所述之一種貴重金屬吸附劑的製作方法,為了取出貴重金屬吸附劑粒子更進一步提出三步驟,其中:步驟(D)係將步驟(C)中之該溶液進行離心程序;步驟(E)該粒子進行過濾及洗滌程序;步驟(F)過濾出之粒子進行乾燥程序。 The method for preparing a precious metal adsorbent according to claim 1, wherein the third step is further carried out in order to take out the precious metal adsorbent particles, wherein: step (D) is to centrifuge the solution in the step (C). Procedure; step (E) the particle is subjected to a filtration and washing procedure; and the step (F) is filtered to remove the particles for a drying procedure. 如申請專利範圍第4項所述之一種貴重金屬吸附劑的製作方法,由單體1係甲基丙烯酸甲酯及單體2係丙烯酸形成粒子為一高分子微球,該粒子之粒徑介於3微米至7微米。 The method for preparing a precious metal adsorbent according to claim 4, wherein the monomer 1 type methyl methacrylate and the monomer 2 type acrylic acid form a polymer microsphere, and the particle size is From 3 microns to 7 microns.
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CN1037848A (en) * 1988-04-28 1989-12-13 住友化学工业株式会社 Metal ion adsorbent and with the method for its adsorbing metal ions
US5328935A (en) * 1993-03-26 1994-07-12 The Procter & Gamble Company Method of makig a superabsorbent polymer foam
TW200932348A (en) * 2008-01-24 2009-08-01 Forestry Bureau Council Of Agriculture Executive Yuan Heavy metal adsorbent and fabrication method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1037848A (en) * 1988-04-28 1989-12-13 住友化学工业株式会社 Metal ion adsorbent and with the method for its adsorbing metal ions
US5328935A (en) * 1993-03-26 1994-07-12 The Procter & Gamble Company Method of makig a superabsorbent polymer foam
TW200932348A (en) * 2008-01-24 2009-08-01 Forestry Bureau Council Of Agriculture Executive Yuan Heavy metal adsorbent and fabrication method thereof

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