CN102019167A - Functionalized mesoporous molecular sieve and application of functionalized mesoporous molecular sieve in recovering noble metal - Google Patents
Functionalized mesoporous molecular sieve and application of functionalized mesoporous molecular sieve in recovering noble metal Download PDFInfo
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- 239000002808 molecular sieve Substances 0.000 title claims abstract description 113
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 113
- 229910000510 noble metal Inorganic materials 0.000 title claims description 34
- -1 palladium ions Chemical class 0.000 claims abstract description 53
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 53
- 229910052737 gold Inorganic materials 0.000 claims abstract description 39
- 239000010931 gold Substances 0.000 claims abstract description 39
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 37
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 37
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 34
- 229910052751 metal Inorganic materials 0.000 claims abstract description 28
- 239000002184 metal Substances 0.000 claims abstract description 28
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 26
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000002699 waste material Substances 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 12
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 5
- 239000010703 silicon Substances 0.000 claims abstract description 5
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 21
- 239000000843 powder Substances 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 8
- FDWREHZXQUYJFJ-UHFFFAOYSA-M gold monochloride Chemical compound [Cl-].[Au+] FDWREHZXQUYJFJ-UHFFFAOYSA-M 0.000 claims description 7
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- MUJIDPITZJWBSW-UHFFFAOYSA-N palladium(2+) Chemical compound [Pd+2] MUJIDPITZJWBSW-UHFFFAOYSA-N 0.000 claims description 5
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 claims description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 4
- SUVIGLJNEAMWEG-UHFFFAOYSA-N propane-1-thiol Chemical compound CCCS SUVIGLJNEAMWEG-UHFFFAOYSA-N 0.000 claims description 4
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical compound CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
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- 239000000203 mixture Substances 0.000 claims 1
- 238000006396 nitration reaction Methods 0.000 claims 1
- NICDRCVJGXLKSF-UHFFFAOYSA-N nitric acid;trihydrochloride Chemical compound Cl.Cl.Cl.O[N+]([O-])=O NICDRCVJGXLKSF-UHFFFAOYSA-N 0.000 claims 1
- 229910052755 nonmetal Inorganic materials 0.000 claims 1
- 239000010970 precious metal Substances 0.000 abstract description 27
- 238000001179 sorption measurement Methods 0.000 abstract description 27
- 238000011084 recovery Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 3
- 125000003396 thiol group Chemical group [H]S* 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 125000003277 amino group Chemical group 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 56
- 150000002500 ions Chemical class 0.000 description 19
- 125000000524 functional group Chemical group 0.000 description 13
- 229910021645 metal ion Inorganic materials 0.000 description 9
- 150000002739 metals Chemical class 0.000 description 9
- 238000000926 separation method Methods 0.000 description 8
- 238000003756 stirring Methods 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- RJHLTVSLYWWTEF-UHFFFAOYSA-K gold trichloride Chemical compound Cl[Au](Cl)Cl RJHLTVSLYWWTEF-UHFFFAOYSA-K 0.000 description 3
- 239000011133 lead Substances 0.000 description 3
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- 229910003771 Gold(I) chloride Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 2
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- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
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Abstract
本发明公开了一种功能化介孔分子筛及其在贵金属回收中的应用。所述的功能化介孔分子筛为嫁接有胺基或巯基的硅系介孔分子筛,其在从废弃电子线路板中回收贵金属中的应用包括如下步骤:将废弃电子线路板处理得到金属溶解液,先调节金属溶解液的pH值到1左右,利用功能化介孔分子筛选择性吸附其中的钯离子和/或铂离子;然后调节金属溶解液pH值为2.5左右,利用功能性分子筛选择性吸附其中的金;用3~6M盐酸分别清洗载有钯离子和/或铂离子的分子筛和载金分子筛,即可使贵金属脱附进入溶液中,同时分子筛重新活化。本发明所述的回收贵金属的方法工艺简单,贵金属吸附率高,同时具有环保优势。The invention discloses a functionalized mesoporous molecular sieve and its application in precious metal recovery. The functionalized mesoporous molecular sieve is a silicon-based mesoporous molecular sieve grafted with amino groups or mercapto groups, and its application in recovering precious metals from waste electronic circuit boards includes the following steps: processing waste electronic circuit boards to obtain a metal solution, First adjust the pH value of the metal solution to about 1, and use functionalized mesoporous molecular sieves to selectively adsorb palladium ions and/or platinum ions; then adjust the pH value of the metal solution to about 2.5, and use functional molecular sieves to selectively adsorb them gold; wash the molecular sieves loaded with palladium ions and/or platinum ions and gold-loaded molecular sieves with 3-6M hydrochloric acid, respectively, so that the precious metals can be desorbed into the solution, and the molecular sieves can be reactivated at the same time. The method for recovering precious metals in the present invention has simple process, high adsorption rate of precious metals and environmental protection advantages.
Description
一、技术领域:1. Technical field:
本发明具体涉及一种嫁接功能基团氨基或巯基的介孔分子筛及其在从废弃电子线路板中贵金属回收如金、钯、铂等贵金属的应用。 The invention specifically relates to a mesoporous molecular sieve grafted with functional group amino or mercapto and its application in recovering precious metals such as gold, palladium, platinum and the like from waste electronic circuit boards. the
三、背景技术:3. Background technology:
据有关统计数据表明,在废弃的电子线路板中含有相当高的金属,一般在20~40%,特别是贵金属含量相当高,是天然矿藏的几十倍甚至几百倍。其中包含3~8%的金,0.1~1%的铂和钯,当然还有含量不等的铜、锡、铝、镍、铅等金属。从金、铂和钯等贵金属的含量来看,从废弃的电子线路板中回收贵金属具有很大的经济效益,其回收的关键是如何把贵金属从其他金属中分离出来并富集。 According to relevant statistical data, the discarded electronic circuit boards contain quite high metals, generally 20-40%, especially precious metals, which are dozens or even hundreds of times that of natural mineral deposits. It contains 3-8% gold, 0.1-1% platinum and palladium, and of course copper, tin, aluminum, nickel, lead and other metals with varying contents. Judging from the content of precious metals such as gold, platinum and palladium, the recovery of precious metals from waste electronic circuit boards has great economic benefits. The key to the recovery is how to separate and enrich precious metals from other metals. the
常见的分子筛(如SBA-15、MCM-41)是具有排列有序介孔结构的新型纳米功能材料,其孔道大小均一、孔径在2-50nm范围内可调,有较高的比表面积,其BET比表面积一般可达到1000m2/g左右。这些特性使介孔分子筛在大分子吸附、催化反应、药物运输等领域有很好的应用前景。但这些分子筛在水溶液中对贵金属离子没有吸附作用。 Common molecular sieves (such as SBA-15, MCM-41) are new nano-functional materials with ordered mesoporous structures. The BET specific surface area can generally reach about 1000m 2 /g. These characteristics make mesoporous molecular sieves have good application prospects in the fields of macromolecule adsorption, catalytic reaction, and drug delivery. However, these molecular sieves have no adsorption effect on noble metal ions in aqueous solution.
因此,设计一种在水溶液中对贵金属离子具有选择性吸附作用的分子筛以实现贵金属与一般金属分离和富集很有意义。 Therefore, it is meaningful to design a molecular sieve that can selectively adsorb noble metal ions in aqueous solution to achieve the separation and enrichment of noble metals from common metals. the
三、发明内容:3. Contents of the invention:
本发明要解决的首要技术问题在于提供一种能高度选择性吸附 贵金属的功能化介孔分子筛。 The primary technical problem to be solved by the present invention is to provide a functionalized mesoporous molecular sieve capable of highly selectively adsorbing precious metals. the
针对上述技术问题,本发明的研究思路为:充分利用SBA-15、MCM-41等介孔分子筛比表面积大的优势,通过在介孔结构上嫁接上一些吸附贵金属离子功能基团(如-NH2或-SH),从而具有选择性吸附贵金属的功能。 In view of the above-mentioned technical problems, the research idea of the present invention is: make full use of the advantages of the large specific surface area of mesoporous molecular sieves such as SBA-15 and MCM-41, and graft some functional groups (such as -NH 2 or -SH), thus having the function of selectively adsorbing noble metals.
本发明具体采用如下技术方案: The present invention specifically adopts the following technical solutions:
一种功能化介孔分子筛,通过如下方法制得:将硅系介孔分子筛置于含有0.1~0.5mol/L氨基丙烷或丙硫醇的无水甲苯中于100~120℃回流12~24小时,然后过滤并在150~180℃温度下干燥以蒸发甲苯,得到胺基或巯基功能化介孔分子筛。 A functionalized mesoporous molecular sieve, prepared by the following method: placing a silicon-based mesoporous molecular sieve in anhydrous toluene containing 0.1-0.5 mol/L aminopropane or propanethiol at 100-120°C for 12-24 hours under reflux , and then filtered and dried at a temperature of 150-180° C. to evaporate toluene to obtain amine- or mercapto-functionalized mesoporous molecular sieves. the
所述的硅系介孔分子筛优选SBA-15或MCM-41介孔分子筛,更优选MCM-41介孔分子筛。 The silicon-based mesoporous molecular sieve is preferably SBA-15 or MCM-41 mesoporous molecular sieve, more preferably MCM-41 mesoporous molecular sieve. the
本发明所制得的功能化介孔分子筛,在酸性条件下能高选择性吸附金离子、铂离子和钯离子,并且胺基功能化介孔分子筛的吸附能力相较于巯基功能化介孔分子筛要更好一些。 The functionalized mesoporous molecular sieve prepared by the present invention can highly selectively adsorb gold ions, platinum ions and palladium ions under acidic conditions, and the adsorption capacity of the amino functionalized mesoporous molecular sieve is higher than that of the sulfhydryl functionalized mesoporous molecular sieve Be better. the
本发明要解决的第二个技术问题在于将所述的功能化介孔分子筛应用于从废弃电子线路板中回收金、铂和钯等贵金属。 The second technical problem to be solved by the present invention is to apply the functionalized mesoporous molecular sieve to recover precious metals such as gold, platinum and palladium from waste electronic circuit boards. the
针对上述技术问题,本发明的研究思路为:利用嫁接有能吸附贵金属离子的功能基团(如-NH2或-SH)的介孔分子筛在酸性溶液中选择性地吸附贵金属离子,在一定条件下不吸附其他金属离子的特点,有效地将贵金属离子与一般金属离子分离;同时通过调节溶液的pH值,使吸附在分子筛上的贵金属离子脱附,实现贵金属离子的富集和分子筛的重新活化。 In view of the above-mentioned technical problems, the research idea of the present invention is: utilize mesoporous molecular sieve grafted with functional groups (such as -NH2 or -SH) capable of adsorbing noble metal ions to selectively adsorb noble metal ions in acidic solution, under certain conditions The characteristics of not adsorbing other metal ions can effectively separate noble metal ions from common metal ions; at the same time, by adjusting the pH value of the solution, the noble metal ions adsorbed on the molecular sieve can be desorbed to achieve the enrichment of noble metal ions and the reactivation of molecular sieves. .
本发明所述的从废弃电子线路板中回收金、铂和钯等贵金属的技 术方案具体如下: The technical scheme of recovering precious metals such as gold, platinum and palladium from waste electronic circuit boards of the present invention is specifically as follows:
所述的回收方法包括如下步骤: Described recovery method comprises the steps:
(a)将废弃电子线路板粉碎、分离得到非金属粉末和金属粉末,将金属粉末用强酸溶解,所得金属溶解液中含有铂离子和钯离子中的一种或两种以及金离子; (a) Pulverizing and separating the waste electronic circuit board to obtain non-metallic powder and metal powder, dissolving the metal powder with strong acid, and containing one or both of platinum ions and palladium ions and gold ions in the metal solution obtained;
(b)调节金属溶解液的pH值到1左右,将功能化介孔分子筛放入金属溶解液中,在室温下搅拌8~12小时,过滤得到相应的载有铂离子和/或钯离子的分子筛和滤液A;本申请制得的功能化介孔分子筛在pH为1左右,对于铂离子和钯离子均能高度选择性吸附,而金离子和其他金属离子则继续留在滤液A中,故根据金属溶液中贵金属离子成分的不同,得到相应的载有铂离子或者钯离子或者铂离子和钯离子的分子筛。 (b) adjust the pH value of the metal solution to about 1, put the functionalized mesoporous molecular sieve into the metal solution, stir at room temperature for 8 to 12 hours, and filter to obtain the corresponding platinum ion and/or palladium ion Molecular sieve and filtrate A; the functionalized mesoporous molecular sieve prepared by the application has a pH of about 1, and can highly selectively adsorb platinum ions and palladium ions, while gold ions and other metal ions continue to remain in filtrate A, so According to the different components of noble metal ions in the metal solution, corresponding molecular sieves loaded with platinum ions or palladium ions or platinum ions and palladium ions are obtained. the
(c)用3~6M盐酸(优选5M盐酸)清洗载有铂离子和/或钯离子的分子筛,过滤得到氯化铂和/或氯化钯溶液和重新活化的功能化介孔分子筛; (c) wash the molecular sieve loaded with platinum ions and/or palladium ions with 3-6M hydrochloric acid (preferably 5M hydrochloric acid), filter to obtain platinum chloride and/or palladium chloride solution and reactivated functionalized mesoporous molecular sieve;
(d)调节滤液A的pH值到2.5左右,将功能化介孔分子筛放入滤液A中,在室温下搅拌8~12小时,过滤得到载金分子筛,用3~6M盐酸(优选5M盐酸)清洗载金分子筛,过滤得到氯化金溶液和重新活化的功能化介孔分子筛。本发明制得的功能化介孔分子筛,在pH值为2.5左右时,能选择性吸附金离子,其他金属离子则继续留在滤液中,从而实现贵金属离子与其他一般离子的分离。 (d) Adjust the pH value of the filtrate A to about 2.5, put the functionalized mesoporous molecular sieve into the filtrate A, stir at room temperature for 8-12 hours, filter to obtain the gold-loaded molecular sieve, and use 3-6M hydrochloric acid (preferably 5M hydrochloric acid) The gold-loaded molecular sieve is cleaned, and the gold chloride solution and the reactivated functionalized mesoporous molecular sieve are obtained by filtering. The functionalized mesoporous molecular sieve prepared by the invention can selectively adsorb gold ions when the pH value is about 2.5, while other metal ions remain in the filtrate, thereby realizing the separation of noble metal ions from other common ions. the
在上述回收方法中,将废弃电子线路板破碎后,可采用超细粉碎机进行粉碎,然后用高压静电分离机分离得到以玻璃纤维、树脂为主的非金属粉末和以铜、锡、铅、金、铂、钯(关于铂和钯,有的电子 线路板中可能只含有铂或者只含有钯)等为主的金属粉末。 In the above recovery method, after the waste electronic circuit board is crushed, it can be pulverized by an ultra-fine pulverizer, and then separated by a high-voltage electrostatic separator to obtain non-metallic powder mainly composed of glass fiber and resin and copper, tin, lead, Gold, platinum, palladium (for platinum and palladium, some electronic circuit boards may only contain platinum or only palladium) and other metal powders. the
上述回收贵金属的方案中,步骤(a)所述的强酸用以溶解金属粉末,优选使用体积比2∶1的浓硝酸和浓盐酸的混酸或者王水。步骤(b)和步骤(d)中调节pH值可使用氢氧化钠溶液等常用碱液。载有铂离子和/或钯离子的分子筛和载金分子筛通过3~6M盐酸溶液处理,优选通过5M盐酸溶液处理,即可使得吸附在分子筛上的贵金属脱附,进入溶液中,同时分子筛重新活化,可重复使用。至于得到的氯化钯溶液、氯化铂溶液或者氯化钯和氯化铂的混合溶液则可通过电解等现有工艺制得相应的贵金属铂和钯;当得到的是氯化钯和氯化铂的混合溶液时,通过在电解过程中控制电位的不同即可分别得到钯和铂。而氯化金溶液可以采用湿法冶金技术电解得到纯度为99.99%的金。 In the above solution for recovering precious metals, the strong acid described in step (a) is used to dissolve the metal powder, preferably a mixed acid of concentrated nitric acid and concentrated hydrochloric acid or aqua regia with a volume ratio of 2:1. Common lyes such as sodium hydroxide solution can be used to adjust the pH value in step (b) and step (d). Molecular sieves and gold-loaded molecular sieves loaded with platinum ions and/or palladium ions are treated with 3-6M hydrochloric acid solution, preferably 5M hydrochloric acid solution, so that the precious metals adsorbed on the molecular sieves can be desorbed and enter the solution, while the molecular sieves are reactivated ,reusable. As for the palladium chloride solution obtained, the platinum chloride solution or the mixed solution of palladium chloride and platinum chloride, the corresponding precious metal platinum and palladium can be produced by existing processes such as electrolysis; In the mixed solution of platinum, palladium and platinum can be obtained respectively by controlling the difference in potential during the electrolysis process. The gold chloride solution can be electrolyzed by hydrometallurgy technology to obtain gold with a purity of 99.99%. the
另外,由于本发明制得的功能化介孔分子筛在不同条件下对于贵金属离子具有其吸附容量,本领域技术人员在实际操作过程中,可以根据矿浆液中的贵金属离子含量和功能化介孔分子筛的吸附容量确定两者的用量比例。 In addition, since the functionalized mesoporous molecular sieve prepared by the present invention has its adsorption capacity for noble metal ions under different conditions, those skilled in the art can, according to the content of noble metal ions in the ore slurry and the functionalized mesoporous molecular sieve The adsorption capacity determines the dosage ratio of the two. the
与现有技术相比,本发明采用能选择性吸附贵金属的功能化介孔分子筛来回收贵金属,工艺简单,仅简单地调整溶液的酸度即能达到贵金属离子分离、解析和富集的目的;功能化介孔分子筛的吸附效率高,其吸附金离子的效率达到98%以上,吸附钯离子和铂离子的效率也在90%以上;本发明的回收过程不涉及剧毒物质,具有环保优势。 Compared with the prior art, the present invention adopts the functionalized mesoporous molecular sieve capable of selectively adsorbing precious metals to recover precious metals, the process is simple, and the purpose of separation, analysis and enrichment of precious metal ions can be achieved only by simply adjusting the acidity of the solution; the function The adsorption efficiency of the mesoporous molecular sieve is high, and its adsorption efficiency of gold ions is over 98%, and the efficiency of adsorption of palladium ions and platinum ions is also over 90%. The recovery process of the present invention does not involve highly toxic substances, and has the advantage of environmental protection. the
四、附图说明4. Description of drawings
图1为本发明实施例三中利用SH-MCM-41从废弃电子线路板中 回收贵金属的工艺流程图。 Fig. 1 is the process flow diagram of utilizing SH-MCM-41 to reclaim precious metals from waste electronic circuit boards in the third embodiment of the present invention. the
五、具体实施方式5. Specific implementation
下面以具体实施例对本发明的技术方案做进一步说明,但本发明的保护范围不限于此: Technical scheme of the present invention will be further described below with specific embodiment, but protection scope of the present invention is not limited to this:
实施例一: Embodiment one:
1、功能基团的嫁接 1. Grafting of functional groups
将2.5g MCM-41粉末放入在含有0.1mol/L氨基丙烷(C3H7NH2)250毫升的无水甲苯中,在120℃温度下回流18小时,在分子筛上嫁接功能基团-NH2,然后过滤提到MCM-41粉末,并将该粉末在110℃温度下干燥12小时以蒸发完全甲苯,得到NH2-MCM-41选择性吸附贵金属功能分子筛。采用同样的方法嫁接功能基团-SH,得到SH-MCM-41选择性吸附贵金属功能分子筛。制得的NH2-MCM-41、SH-MCM-41的物化性能见表1。 Put 2.5g of MCM-41 powder into 250ml of anhydrous toluene containing 0.1mol/L aminopropane (C 3 H 7 NH 2 ), reflux at 120°C for 18 hours, and graft functional groups on molecular sieves- NH 2 , then filter the MCM-41 powder, and dry the powder at 110° C. for 12 hours to evaporate the toluene completely to obtain the NH 2 -MCM-41 selective adsorption noble metal functional molecular sieve. Using the same method to graft the functional group -SH, the SH-MCM-41 selective adsorption noble metal functional molecular sieve was obtained. The physical and chemical properties of the prepared NH 2 -MCM-41 and SH-MCM-41 are shown in Table 1.
2、贵金属的选择性吸附和脱附 2. Selective adsorption and desorption of precious metals
将50g NH2-MCM-41选择性吸附贵金属功能分子筛放入2.5升含有276g氯化金(AuCl3)和59g氯化钯(PdCl3)的溶液中,将溶液的pH值调整到1.0,在室温下搅拌2小时后过滤出载有贵金属离子的分子筛,测定溶液中金、钯离子的含量。然后用5M HCl溶液清洗载有贵金属离子的分子筛,得到只含有PdCl3的溶液和解析下来的分子筛。再一次将功能分子筛放入含有上一次过滤后的溶液中,将溶液的pH值调整到2.5,同样在室温下搅拌2小时后过滤载有金离子的分子筛,测定溶液中金、钯离子的含量。并用5M HCl溶液清洗载有金离子的分子筛,得到AuCl3溶液和分子筛,分子筛可以再一次利用。 Put 50g NH 2 -MCM-41 selective adsorption noble metal functional molecular sieve into 2.5 liters of solutions containing 276g gold chloride (AuCl 3 ) and 59g palladium chloride (PdCl 3 ), adjust the pH value of the solution to 1.0, and After stirring at room temperature for 2 hours, filter out the molecular sieve loaded with noble metal ions, and measure the content of gold and palladium ions in the solution. Then the molecular sieve loaded with noble metal ions was washed with 5M HCl solution to obtain a solution containing only PdCl3 and the resolved molecular sieve. Put the functional molecular sieve into the solution containing the last filtration again, adjust the pH value of the solution to 2.5, filter the molecular sieve loaded with gold ions after stirring at room temperature for 2 hours, and measure the content of gold and palladium ions in the solution . And wash the molecular sieve loaded with gold ions with 5M HCl solution to obtain AuCl 3 solution and molecular sieve, the molecular sieve can be used again.
同样,采用SH-MCM-41为选择性吸附贵金属功能分子筛进行贵金属的选择性吸附和分离。 Similarly, SH-MCM-41 is used as a functional molecular sieve for selective adsorption of noble metals for selective adsorption and separation of noble metals. the
NH2-MCM-41、SH-MCM-41的吸附性能见表1。 The adsorption properties of NH 2 -MCM-41 and SH-MCM-41 are shown in Table 1.
表1:嫁接功能基团前后介孔分子筛的物理、化学和吸附性能 Table 1: Physical, chemical and adsorption properties of mesoporous molecular sieves before and after grafting functional groups
表1是三种不同分子筛的物理、化学和吸附贵金属离子性能的情况。从N2低温吸附试验结果可以看到,-NH2或-SH基团在分子筛表面上嫁接的同时,也在分子筛介孔内壁上成功嫁接,使得介孔分子筛的内径变小,如嫁接上-NH2基团后,内径从3.09nm减少到2.92nm,这样,嫁接功能基团前后分子筛的比表面积有所减少,BET比表面从1140m2/g减少到774m2/g,但没有嫁接功能基团的分子筛都不具备吸附贵金属离子的作用,而嫁接了功能基团的分子筛在酸性溶液中具有选择性较强高效吸附贵金属的能力。从吸附试验结果可以看到,NH2-MCM-41分子筛几乎能吸附溶液中所有贵金属离子,溶液中100%的金离子和99.2%钯离子被吸附;而且简单地把溶液的pH从1.0调整到2.5,就能较好地实现金和钯离子的分离。与NH2-MCM-41分子筛相比,SH-MCM-41分子筛的吸附能力稍差一些。采用SH-MCM-41分子筛,溶液中99.3%的金离子和91.9%钯离子能有效地被吸附并分离。 Table 1 shows the physical, chemical and adsorption properties of noble metal ions of three different molecular sieves. From the results of N 2 low temperature adsorption test, it can be seen that while -NH 2 or -SH groups are grafted on the surface of the molecular sieve, they are also successfully grafted on the inner wall of the mesoporous molecular sieve, making the inner diameter of the mesoporous molecular sieve smaller, such as grafting on the - After adding NH 2 groups, the inner diameter decreases from 3.09nm to 2.92nm, so that the specific surface area of molecular sieves before and after grafting functional groups decreases, and the BET specific surface decreases from 1140m 2 /g to 774m 2 /g, but there is no grafting of functional groups Molecular sieves with agglomerates do not have the effect of adsorbing noble metal ions, but molecular sieves grafted with functional groups have a strong selective and efficient ability to adsorb noble metals in acidic solutions. As can be seen from the adsorption test results, the NH 2 -MCM-41 molecular sieve can almost adsorb all noble metal ions in the solution, and 100% of the gold ions and 99.2% of the palladium ions in the solution are adsorbed; and simply adjust the pH of the solution from 1.0 to 2.5, the separation of gold and palladium ions can be achieved better. Compared with NH 2 -MCM-41 molecular sieve, the adsorption capacity of SH-MCM-41 molecular sieve is slightly worse. Using SH-MCM-41 molecular sieve, 99.3% of gold ions and 91.9% of palladium ions in the solution can be effectively adsorbed and separated.
实施例二:利用SBA-15分子筛嫁接功能基团并在分离金和铂中的应用 Example 2: Using SBA-15 molecular sieve to graft functional groups and its application in separating gold and platinum
1、功能基团的嫁接 1. Grafting of functional groups
将2.5g SBA-15粉末放入在含有0.1mol/L氨基丙烷(C3H7NH2)250毫升的无水甲苯中,在120℃温度下回流18小时,在分子筛上嫁接功能基团-NH2,然后过滤提到SBA-15粉末,并将该粉末在110℃温度下干燥12小时以蒸发完全甲苯,得到NH2-SBA-15选择性吸附贵金属功能分子筛。 Put 2.5g of SBA-15 powder into 250ml of anhydrous toluene containing 0.1mol/L aminopropane (C 3 H 7 NH 2 ), reflux at 120°C for 18 hours, and graft functional groups on molecular sieves- NH 2 , then filter the SBA-15 powder, and dry the powder at 110° C. for 12 hours to evaporate the toluene completely to obtain the NH 2 -SBA-15 selective adsorption noble metal functional molecular sieve.
2、金、铂的选择性吸附和分离 2. Selective adsorption and separation of gold and platinum
将25g NH2-SBA-15选择性吸附贵金属功能分子筛放入2升含有76g氯化金(AuCl3)和24g氯化铂(PtCl3)的溶液中,将溶液的pH值调整到1.0,在室温下搅拌2小时后过滤出载有金和铂离子的功能分子筛,测定溶液中金、铂离子的含量。然后用5M HCl溶液清洗载有贵金属离子的分子筛,得到只含有PtCl3的溶液和解析下来的分子筛。再一次将功能分子筛放入含有上一次过滤后的溶液中,将溶液的pH值调整到2.5,同样在室温下搅拌2小时后过滤载有金离子的分子筛,测定溶液中金、铂离子的含量,并用5M HCl溶液清洗载有金离子的分子筛,得到AuCl3溶液和分子筛,吸附结果见表2。结果表明,通过调节溶液的pH值,NH2-SBA-15达到分离和富集金和铂的目的。5M HCl溶液清洗下来的分子筛可以再利用。 Put 25g NH 2 -SBA-15 selective adsorption precious metal functional molecular sieve into 2 liters of solutions containing 76g gold chloride (AuCl 3 ) and 24g platinum chloride (PtCl 3 ), adjust the pH value of the solution to 1.0, and After stirring at room temperature for 2 hours, the functional molecular sieve loaded with gold and platinum ions was filtered out, and the content of gold and platinum ions in the solution was measured. Then the molecular sieve loaded with noble metal ions was washed with 5M HCl solution to obtain a solution containing only PtCl3 and the molecular sieve that was resolved. Put the functional molecular sieve into the solution containing the last filtration again, adjust the pH value of the solution to 2.5, also filter the molecular sieve loaded with gold ions after stirring at room temperature for 2 hours, and measure the content of gold and platinum ions in the solution , and the molecular sieve loaded with gold ions was washed with 5M HCl solution to obtain AuCl 3 solution and molecular sieve. The adsorption results are shown in Table 2. The results show that NH 2 -SBA-15 achieves the purpose of separating and enriching gold and platinum by adjusting the pH value of the solution. The molecular sieves washed with 5M HCl solution can be reused.
表2:嫁接功能基团前后SBA-15的物理性能及吸附分离 Table 2: Physical properties and adsorption separation of SBA-15 before and after grafting functional groups
实施例三: Embodiment three:
选择性吸附贵金属功能分子筛从废弃电子线路板中回收贵金属。将废弃的手机电子线路板粉碎,超微粉碎和高压静电分离,得到的金属粉末经体积比1∶2的浓盐酸∶浓硝酸溶解后得到的含有金属离子的溶液。溶液中含有金0.015mol;铂0.009mol;铜0.47mol;锡0.21mol;铅0.077mol;铁0.27mol;镍0.17mol。用氢氧化钠溶液将溶解液的pH值调整到1.0左右,将5g SH-MCM-41分子筛放入金属溶解液中,在室温下搅拌12小时,让分子筛充分吸附贵金属离子。过滤溶液后得到载有贵金属离子的分子筛和含有未吸附金属的溶解液。 Selective adsorption of precious metal functional molecular sieves for recovery of precious metals from waste electronic circuit boards. Discarded mobile phone electronic circuit boards are pulverized, superfinely pulverized and separated by high-voltage electrostatics, and the obtained metal powder is dissolved in concentrated hydrochloric acid:concentrated nitric acid with a volume ratio of 1:2 to obtain a solution containing metal ions. The solution contains 0.015mol of gold; 0.009mol of platinum; 0.47mol of copper; 0.21mol of tin; 0.077mol of lead; 0.27mol of iron; Use sodium hydroxide solution to adjust the pH value of the solution to about 1.0, put 5g SH-MCM-41 molecular sieve into the metal solution, and stir at room temperature for 12 hours to allow the molecular sieve to fully absorb noble metal ions. After filtering the solution, molecular sieves loaded with precious metal ions and a solution containing unadsorbed metals are obtained. the
采用5M HCl清洗载贵金属分子筛,得到0.009氯化铂(即100%的铂离子)和0.0002mol的氯化金(1.3%的金离子)。含有未吸附金属的溶解液中已经没有铂离子,说明铂离子已经被功能分子筛吸附而分离,而大部分金离子和其他金属仍留在溶解液中。 Adopt 5M HCl to wash loaded noble metal molecular sieve, obtain 0.009 platinum chloride (being 100% platinum ion) and the gold chloride of 0.0002mol (1.3% gold ion). There are no platinum ions in the solution containing unadsorbed metals, indicating that the platinum ions have been adsorbed and separated by the functional molecular sieve, while most of the gold ions and other metals remain in the solution. the
将过滤后得到的溶解液pH值调整到2.5左右,把经上述经5MHCl清洗后的分子筛重新放入金属溶解液中,在室温下搅拌12小时,让分子筛充分吸附金属离子。经过滤后得到载有0.0148mol的氯化金(AuCl3)和微量的其他金属(Cu和Ni)的分子筛和含有未吸附金属的溶解液,这样实现了金离子与其他金属离子的分离。然后,再采用5M HCl清洗载金功能分子筛,得到氯化金溶液,过滤后得到的功能分子筛还可以重新用于吸附贵金属。图1显示的是利用SH-MCM-41从废弃电子线路板回收贵金属工艺过程和实施例三的实验数据。 Adjust the pH value of the solution obtained after filtration to about 2.5, put the molecular sieve washed with 5M HCl into the metal solution again, and stir at room temperature for 12 hours to allow the molecular sieve to fully absorb metal ions. After filtering, a molecular sieve loaded with 0.0148 mol of gold chloride (AuCl 3 ) and trace amounts of other metals (Cu and Ni) and a solution containing unadsorbed metals are obtained, thereby realizing the separation of gold ions from other metal ions. Then, the gold-loaded functional molecular sieve is washed with 5M HCl to obtain a gold chloride solution, and the functional molecular sieve obtained after filtration can be reused for adsorbing precious metals. Figure 1 shows the process of recovering precious metals from waste electronic circuit boards using SH-MCM-41 and the experimental data of Example 3.
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CN103112917A (en) * | 2013-01-19 | 2013-05-22 | 桂林理工大学 | Method for purifying lead-bearing wastewater |
CN106984364A (en) * | 2016-01-20 | 2017-07-28 | 中国科学院大连化学物理研究所 | Application of the SAPO molecular sieve analog original powder in separated/extracted metal ion |
CN106378117A (en) * | 2016-09-14 | 2017-02-08 | 南昌大学 | Preparation method of mesoporous material and application of mesoporous material in low concentration rare earth ion enrichment and recovery |
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CN112299437A (en) * | 2019-07-31 | 2021-02-02 | 中国石油化工股份有限公司 | Sulfydryl functionalized SBA molecular sieve raw powder, molecular sieve, and preparation methods and applications thereof |
CN112299437B (en) * | 2019-07-31 | 2022-08-19 | 中国石油化工股份有限公司 | Sulfydryl functionalized SBA molecular sieve raw powder, molecular sieve, and preparation methods and applications thereof |
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