CN113058571B - Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery - Google Patents

Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery Download PDF

Info

Publication number
CN113058571B
CN113058571B CN202110307562.0A CN202110307562A CN113058571B CN 113058571 B CN113058571 B CN 113058571B CN 202110307562 A CN202110307562 A CN 202110307562A CN 113058571 B CN113058571 B CN 113058571B
Authority
CN
China
Prior art keywords
gold
bifunctional
tfn
pda
bifunctional polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202110307562.0A
Other languages
Chinese (zh)
Other versions
CN113058571A (en
Inventor
邱建丁
李学晶
梁汝萍
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanchang University
Original Assignee
Nanchang University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nanchang University filed Critical Nanchang University
Priority to CN202110307562.0A priority Critical patent/CN113058571B/en
Publication of CN113058571A publication Critical patent/CN113058571A/en
Application granted granted Critical
Publication of CN113058571B publication Critical patent/CN113058571B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/265Synthetic macromolecular compounds modified or post-treated polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3071Washing or leaching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3085Chemical treatments not covered by groups B01J20/3007 - B01J20/3078
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/70Treatment of water, waste water, or sewage by reduction
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/04Obtaining noble metals by wet processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • C22B3/24Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition by adsorption on solid substances, e.g. by extraction with solid resins
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Manufacturing & Machinery (AREA)
  • Water Supply & Treatment (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention discloses a preparation method of a bifunctional polymer adsorbent and application of the bifunctional polymer adsorbent in gold recovery, and belongs to the technical field of adsorption materials. Dopamine (DA) and Tetrafluoroterephthalonitrile (TFN) are subjected to aromatic nucleophilic reaction to form polymer PDA-TFN, and then cyano is converted into amide under alkaline conditions to prepare bifunctional polymer adsorbent PDA-TFN-A. PDA-TFN-A contains A large number of indole structures and amide functional groups, and can be specifically combined with Au (III) to improve the adsorption quantity. PDA-TFN-A can reduce Au (III) into Au (0), and has good recovery performance on gold. The method for synthesizing the bifunctional polymer is simple, low in cost, environment-friendly, economical and efficient, and is expected to be used for recovering gold in electronic waste liquid through the synergistic effect of adsorption and reduction.

Description

Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery
Technical Field
The invention belongs to the technical field of adsorption materials, and particularly relates to a preparation method of a bifunctional polymer adsorbent and application of the bifunctional polymer adsorbent in gold recovery.
Background
With the advent of economic integration, the electronic industry has become the major strategic development industry of countries around the world with its characteristics of low consumption, no pollution, high added value, etc. It is known that the development of the electronic industry generates a great deal of electronic garbage and electronic equipment waste, wherein the contained precious metals may cause waste (Mon, M.; Ferrando-Soria, J.; Grancha, T.; Fortea-P rez, F.R.; Gascon, J.; Leyva-P rez, A.; Armentano, D.; Pardo, E.Select gold recovery and catalysis in a high grade flexible metal-degraded metal-synthesized metal-7867, J.Am.chem.Soc.2016,138, 7864-7867). Gold is widely used as a popular noble metal in the fields of chemical engineering and the like. Although the gold content in the electronic garbage is far higher than that of natural ore, serious resource waste is caused due to the lack of a high-selectivity, high-yield and environment-friendly extraction technology. Therefore, new technical materials for recovering gold from such electronic wastes are important for the sustainable development of the future (Cao, W.; Dai, F.; Hu, R.; Tang, B.Z. ecological sulfur conversion to functional polyurethanes catalysts of sulfur, acids, and amines.J.Am.chem.Soc.2020,142, 978-986). Methods for recovering gold reported so far include chemical precipitation, redox, solvent extraction, ion exchange, adsorption, and the like. Among them, the chemical precipitation method often causes secondary pollution after treatment, such as generation of a large amount of waste residues, and has negative effects in practical application and ecological environment development (Yue, C.; Sun, H.; Liu, W. -J.; Guan, B.; Deng, X.; Zhang, X.; Yang, P.environmental benign, rapid, and selective extraction of gold from organisms and water electronic materials, Angew.Chem.2017,56, 9331-. Gold is extracted by using the redox principle in industry, and the problems of harsh reaction conditions, serious environmental pollution and high energy consumption exist all the time due to the use of toxic oxidizing reagents. Solvent extraction and ion exchange methods have difficulties with cumbersome operations and low yields (Raiguel, S.; Gijsemanns, L.; Van den Bossche, A.; Onghena, B.; Binnemans, K.solvent extraction of gold (iii) with ethylene carbonate ACS Sustain. chem. Eng.2020,8, 13713. quadrature, M.I.; Hewitt, D.M.; Dai, X.; Brunt, S.D.ion extraction and passage for recovering gold free solutions. hydrometallurgy 2010,100, 136. 143). Adsorption methods that are simple to operate, economical and efficient are of wide interest to researchers (Gurung, m.; Adhikari, b.b.; morsiada, s.; Kawakita, h.; Ohto, k.; Inoue, k.; Alam, S.N-amino modified proton tannin: a new stable material for selective adsorption, preconcentration and recovery of precursors metals from ionic chlorine chloride solution, bioreesor. technol.2013,129, 108-117). Adsorbing materials such as resins, carbon materials, ion imprinting, and activated carbon are widely used for gold recovery, but have the disadvantages of long treatment time, complicated operation, and inability to recycle. Therefore, designing and using an economical, efficient and degradable polymer is of great importance for recovering gold from secondary resources such as waste electrical appliances, electronic equipment and the like.
Dopamine (DA) is a cheap, readily available, biodegradable, environmentally friendly natural biomolecule, Polydopamine (PDA) rich in amino and hydroxyl functional groups, which can form indole units by autopolymerization, with excellent complexing power for metal ions (Sun, D.T.; Pen, L.; Reeder, W.S.; Moosavi, S.M.; Tiana, D.; Britt, D.K.; Oveisi, E.; Queen, W.L.Rapid, selective, heavy metal, reactive, free from water by a metal/polymeric, composite, CeACS. Sci.2018,4, 349-). In order to prevent the dopamine from dissolving in practical application and improve the adsorption performance of the dopamine on Au (III), the dopamine is modified through crosslinking. So far, no report is found for preparing bifunctional polymer adsorbent based on dopamine functionalized derivative for recovering noble metal.
Disclosure of Invention
The invention aims to provide a preparation method of a bifunctional polymer adsorbent and gold recovery application thereof, the method for preparing the bifunctional polymer adsorbent has the characteristics of simple operation, environmental friendliness, economy and high efficiency, has the advantages of high adsorption capacity, rapid adsorption kinetics and high selectivity on gold, and can be used for recovering gold from electronic waste liquid.
The invention provides a preparation method of a bifunctional polymer adsorbent, which comprises the following steps:
1) dopamine and tetrafluoroterephthalonitrile are used as reaction raw materials, anhydrous potassium carbonate is used as a catalyst, anhydrous tetrahydrofuran/N, N-dimethylformamide is added into the reaction raw materials, and a reaction mixed solution is obtained after the anhydrous tetrahydrofuran/N, N-dimethylformamide is uniformly mixed;
2) sealing the reaction mixture liquid, vacuumizing, introducing nitrogen, stirring at 80-90 ℃ for 2-4 days, taking out, cooling to room temperature, and stirring for 20-28h to obtain a reaction mixture;
3) and filtering the reaction mixture, collecting the precipitate, removing impurities from the precipitate, drying in vacuum to obtain a brownish black polymer, and carrying out post-treatment on the polymer under an alkaline condition to obtain the bifunctional polymer adsorbent.
Further, the mass ratio of the dopamine, the tetrafluoroterephthalonitrile and the anhydrous potassium carbonate in the step 1) is (1.8-2.0): 1: (2.6-2.8).
Further, the volume ratio of the tetrahydrofuran to the N, N-dimethylformamide in the anhydrous tetrahydrofuran/N, N-dimethylformamide in the step 1) is (8.5-9.5): 1.
further, step 3) ofThe precipitation and impurity removal is to drop HCl solution until no CO exists2Discharging to remove unreacted potassium carbonate, washing precipitate with water, tetrahydrofuran, N-dimethylformamide and acetone respectively, and performing Soxhlet extraction in tetrahydrofuran and acetone for 22-26 h.
Further, the concentration of the HCl solution is 0.5 mol/L.
Further, the alkaline condition in the step 3) is an aqueous solution of NaOH; the post-treatment is to mix the polymer and NaOH aqueous solution, stir for 2-4 days at 60-80 ℃, filter, separate and wash the product with deionized water, then transfer to a Soxhlet extractor to wash with tetrahydrofuran and acetone for 22-26h, and perform vacuum drying.
Further, the concentration of the NaOH solution is 6 mol/L.
The invention also provides an application of the bifunctional polymer adsorbent in gold adsorption:
and adding the bifunctional polymer adsorbent prepared by the method into a solution to be treated containing gold (III), keeping the temperature constant, oscillating to obtain a suspension, adsorbing by using the bifunctional polymer adsorbent, and reducing the gold (III) in the suspension into gold (0).
Further, the content of gold (III) in the solution to be treated containing gold (III) is 50-2500 ppm; and/or the solution to be treated containing gold (III) is subjected to pH adjustment to 1-9 by adopting a pH adjusting agent before being mixed with the bifunctional polymer adsorbent; preferably, the pH is 2.
Further, the constant temperature is 20-30 ℃; the oscillation time of the adsorption isotherm experiment is 22-26 h; the oscillation time of the kinetic experiment is 2-180 min.
Further, the method also comprises the step of filtering the suspension after adsorption and reduction by using a 0.22 mu m microporous filter membrane.
Compared with the prior art, the invention has the beneficial effects that:
the invention takes dopamine and tetrafluoroterephthalonitrile as raw materials, prepares polymer PDA-TFN through aromatic nucleophilic reaction, and amidates PDA-TFN under alkaline condition to prepare bifunctional polymer adsorbent PDA-TFN-A, PDA-TFN-A contains A large amount of functional groups such as amino, imino and amide, etc., and can be specifically combined with Au (III), thereby improving the adsorption capacity to Au (III); in addition, PDA-TFN-A can also reduce adsorbed Au (III) into Au (0), and has excellent recovery performance on gold. The bifunctional polymer adsorbent designed by the invention has the advantages of simple preparation method, low cost, environmental friendliness, economy and high efficiency, and can be used for recovering gold from electronic waste liquid through the synergistic effect of the efficient adsorption and reduction of the adsorbent on gold.
Drawings
FIG. 1 is A schematic diagram of the preparation of PDA-TFN-A.
FIG. 2 is an SEM image of PDA-TFN-A.
FIG. 3 is an infrared spectrum of DA, TFN, PDA-TFN and PDA-TFN-A.
FIG. 4 is A diagram of the adsorption isotherm of PDA-TFN-A on Au (III).
FIG. 5 is A graph showing the adsorption kinetics of PDA-TFN-A to Au (III).
FIG. 6 is an XRD pattern before and after adsorption of Au (III) by PDA-TFN-A.
FIG. 7 is A graph showing the adsorption selectivity of PDA-TFN-A to Au (III).
Detailed Description
The technical solution of the present invention will be described more clearly and completely with reference to the following examples, which are only a part of the examples of the present invention, but not all of them, which are conventional processes unless otherwise specified, and raw materials which are commercially available from the public unless otherwise specified. All other embodiments, which can be derived by a person skilled in the art from the embodiments of the present invention without making creative efforts, fall within the protection scope of the present invention.
Example 1: preparation method and characterization of bifunctional polymer adsorbent
Placing 1.8964g dopamine, 1.0005g Tetrafluoroterephthalonitrile (TFN) and 2.764g anhydrous potassium carbonate in a three-neck round-bottom flask, adding 80mL anhydrous tetrahydrofuran/N, N-dimethylformamide (9:1v/v), mixing well, sealing, vacuumizing for 20min with a vacuum pump, introducing nitrogen and stirring at 85 ℃ for 3 days under nitrogen atmosphere, taking out and cooling to room temperatureThe nitrogen source was removed, stirring was continued at room temperature for 24h, the mixture was taken out and the precipitate collected by filtration and 0.5mol/L HCl solution was added dropwise until free of CO2Is discharged to remove unreacted K2CO3Washing the precipitate with water, tetrahydrofuran, N-dimethylformamide and acetone respectively, performing Soxhlet extraction in tetrahydrofuran and acetone for 24h, and vacuum drying at 60 ℃ for 12h to obtain a brownish black polymer PDA-TFN; a single neck round bottom flask was charged with 2g of prepared PDA-TFN and 100mL of 6mol/L NaOH solution, the mixture was stirred at 70 ℃ for 3 days, after filtration, separation and washing of the product with deionized water, transferred to A Soxhlet extractor and washed with tetrahydrofuran and acetone, respectively, for 24h, and vacuum dried at 60 ℃ for 8h to produce bifunctional polymer adsorbent PDA-TFN-A. FIG. 1 is A schematic diagram of the preparation process of PDA-TFN-A.
The morphology of PDA-TFN-A is observed by A Scanning Electron Microscope (SEM) (figure 2), and the result of the SEM shows that the bifunctional polymer adsorbent PDA-TFN-A presents A random rough surface. FIG. 3 is an infrared spectrum of DA, TFN, PDA-TFN and PDA-TFN-A, and it was found by comparing the infrared spectrA of DA and TFN that the infrared spectrum of PDA-TFN formed after chemical crosslinking of DA and TFN was 1112cm in the infrared spectrum-1A new stretching vibration peak appears, which is attributed to newly generated aromatic ether bonds, and TFN 1319cm is observed-1The C-F bond at (C-F) disappeared while the cyano group of TFN (2222 cm) was retained-1) Thus, the synthesis of PDA-TFN was successful. After amidation of PDA-TFN under alkaline condition, cyano group (2217 cm) in infrared spectrum of PDA-TFN-A is generated-1) Disappeared at 1667cm-1And A new carbonyl (C ═ O) stretching vibration peak appears, and the results show that the bifunctional polymer adsorbent PDA-TFN-A is successfully prepared by the method.
Example 2: application of bifunctional polymer adsorbent in gold adsorption
The pH of the au (iii) solution was optimized. The result shows that the adsorption efficiency of the bifunctional polymer adsorbent PDA-TFN-A to Au (III) is the maximum when the pH value of the Au (III) solution is 2.0. When the pH of the solution is higher than 5.0, the efficiency of adsorption of Au (III) by PDA-TFN-A is low due to OH in the chloride aqueous solution-With Cl-Compete for the formation of hydroxyl-containing gold complexes. Therefore, the optimum reaction pH for the aqueous Au (III) solution was chosen to be 2.0.
The adsorption capacity and adsorption kinetic behavior of the bifunctional polymer adsorbent PDA-TFN-A on Au (III) were studied. Dissolving potassium chloroaurate in ultrapure water to prepare Au (III) solutions with different concentrations, adjusting the pH value of the solution to 2.0 by using HCl or NaOH, adding 5mg of PDA-TFN-A into 20mL of the Au (III) aqueous solution after the pH value is adjusted, oscillating the solution in A thermostatic water bath for 24 hours, separating precipitates by using A0.22 mu m membrane filter, measuring the concentration of the residual Au (III) in the filtrate by using an inductively coupled plasmA mass spectrometry (ICP-MS), and calculating the adsorption amount of the PDA-TFN-A to the Au (III). Due to the larger driving force of the solid-liquid interface concentration gradient, the adsorption capacity of the PDA-TFN-A to the Au (III) is increased along with the increase of the Au (III) concentration until the adsorption equilibrium is reached, and the maximum adsorption capacity of the PDA-TFN-A to the Au (III) is 2771.8mg/g (figure 4). The adsorption capacity of the PDA-TFN-A to Au (III) is increased along with the prolonging of the adsorption time, when the adsorption time is within 10min, the adsorption capacity is increased sharply along with the prolonging of the adsorption time, then the adsorption capacity is increased slowly, and when the adsorption time is 15min, the adsorption capacity of the Au (III) is saturated (figure 5).
The PDA-TFN-A before and after adsorbing Au (III) is characterized by X-ray diffraction spectrum (XRD). From the XRD results, the adsorbents adsorbing Au (iii) showed characteristic diffraction peaks of Au (0) at (111), (200), (220) and (311), respectively, indicating good reduction behavior of PDA-TFN-A to Au (iii) (fig. 6).
The selective adsorption of Au (III) by PDA-TFN-A was investigated. By adding other metal ions (Cd) commonly found in electronic waste liquid2+、Cr2+、Pb2+、Cu2+、Ni2+、Co2+、Na+、K+、Mg2+、Al3+、Zn2+、Hg2+、Ca2+) The results of examining the selectivity of PDA-TFN-A on the adsorption of Au (III) show that the adsorption of PDA-TFN-A on other metal ions is very small, and the adsorption selectivity of PDA-TFN-A on Au (III) is very high (FIG. 7).
Therefore, the bifunctional polymer adsorbent PDA-TFN-A prepared by the method has A synergistic effect of efficient adsorption and reduction on Au (III), and has the advantages of high adsorption capacity, high adsorption speed and good selectivity. The PDA-TFN-A has the best adsorption performance under the acidic condition of pH 2.0, and shows that the PDA-TFN-A has good application potential for recovering gold from the acidic electronic waste liquid.
The above description is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, many modifications and variations can be made without departing from the principle of the present invention, and these modifications and variations should also be considered as included in the protection scope of the present invention.

Claims (9)

1. A method for preparing a bifunctional polymeric adsorbent, comprising:
1) dopamine and tetrafluoroterephthalonitrile are used as reaction raw materials, anhydrous potassium carbonate is used as a catalyst, anhydrous tetrahydrofuran and N, N-dimethylformamide are added into the reaction raw materials, and a reaction mixed solution is obtained after the anhydrous tetrahydrofuran and the N, N-dimethylformamide are uniformly mixed; the volume ratio of the anhydrous tetrahydrofuran to the N, N-dimethylformamide is (8.5-9.5): 1;
2) sealing the reaction mixture liquid, vacuumizing, introducing nitrogen, stirring at 80-90 ℃ for 2-4 days, taking out, cooling to room temperature, and stirring for 20-28h to obtain a reaction mixture;
3) filtering the reaction mixture, collecting the precipitate, removing impurities from the precipitate, drying in vacuum to obtain a brownish black polymer, and carrying out post-treatment on the polymer under an alkaline condition to obtain the bifunctional polymer adsorbent; the alkaline condition is NaOH aqueous solution; the post-treatment is to mix the polymer and NaOH aqueous solution, stir for 2-4 days at 60-80 ℃, filter, separate and wash the product with deionized water, then transfer to a Soxhlet extractor to wash with tetrahydrofuran and acetone for 22-26h, and perform vacuum drying.
2. The method for preparing the bifunctional polymer adsorbent according to claim 1, wherein the mass ratio of the dopamine, the tetrafluoroterephthalonitrile and the anhydrous potassium carbonate in the step 1) is (1.8-2.0): 1: (2.6-2.8).
3. The method for preparing the bifunctional polymer adsorbent according to claim 1, wherein the step 3) of removing impurities is dropwise adding HCl solution until no CO is generated2Discharging, washing the precipitate with water, tetrahydrofuran, N-dimethylformamide and acetone respectively, and performing Soxhlet extraction in tetrahydrofuran and acetone for 22-26 h.
4. Use of the bifunctional polymeric adsorbent obtained by the preparation method of any one of claims 1-3 for adsorbing gold.
5. The application of the bifunctional polymer adsorbent in gold adsorption according to claim 4, wherein the application method comprises the steps of adding the bifunctional polymer adsorbent into a solution to be treated containing trivalent gold, oscillating at constant temperature to obtain a suspension, adsorbing by the bifunctional polymer adsorbent, and reducing trivalent gold in the suspension to zero valent gold.
6. The use of the bifunctional polymeric adsorbent according to claim 5 for adsorbing gold, wherein the trivalent gold content of the solution to be treated containing trivalent gold is 50-2500 ppm; and/or the solution to be treated containing the trivalent gold needs to be adjusted to the pH value of 1-9 by adopting a pH regulator before being mixed with the bifunctional polymer adsorbent.
7. The use of the bifunctional polymeric adsorbent of claim 6 for adsorbing gold, wherein the pH is 2.
8. The use of the bifunctional polymeric adsorbent according to claim 5 for adsorbing gold, wherein the constant temperature is 20-30 ℃; the oscillation time of the adsorption isotherm experiment is 22-26h, and the oscillation time of the kinetic experiment is 2-180 min.
9. The use of the bifunctional polymeric adsorbent of claim 5 for adsorbing gold, further comprising filtering the suspension after adsorption and reduction with a 0.22 μm microporous membrane.
CN202110307562.0A 2021-03-23 2021-03-23 Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery Active CN113058571B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110307562.0A CN113058571B (en) 2021-03-23 2021-03-23 Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110307562.0A CN113058571B (en) 2021-03-23 2021-03-23 Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery

Publications (2)

Publication Number Publication Date
CN113058571A CN113058571A (en) 2021-07-02
CN113058571B true CN113058571B (en) 2022-05-20

Family

ID=76563082

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110307562.0A Active CN113058571B (en) 2021-03-23 2021-03-23 Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery

Country Status (1)

Country Link
CN (1) CN113058571B (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100771089B1 (en) * 2006-04-28 2007-10-29 주식회사 셀텍 Gene analysis method using semmiconductor photodiode array chips
CN108067206A (en) * 2017-11-27 2018-05-25 同济大学 A kind of adsorbent of modified poly-dopamine functionalization and preparation method and application
CN108262025B (en) * 2018-02-26 2020-10-23 南昌大学 Preparation method of porous nano composite material and application of porous nano composite material in heavy metal ion removal
CN108452781A (en) * 2018-04-02 2018-08-28 福州大学 The preparation method of core-shell magnetic gamma-cyclodextrin polymer composites and application
CN112516972B (en) * 2019-09-19 2023-08-25 南京中医药大学 Nanometer material capable of selectively enriching and separating sulfur-containing compounds, and preparation method and application thereof

Also Published As

Publication number Publication date
CN113058571A (en) 2021-07-02

Similar Documents

Publication Publication Date Title
Liu et al. Adsorption of lead (Pb) from aqueous solution with Typha angustifolia biomass modified by SOCl2 activated EDTA
CN110734120B (en) Water treatment method for activating persulfate by nano zero-valent iron and nickel
Zheng et al. Banana peel carbon that containing functional groups applied to the selective adsorption of Au (III) from waste printed circuit boards
CN113214480A (en) Synthesis method and adsorption application of cationic framework material
CN113249574A (en) Method for recovering aluminum in waste positive plate by utilizing selective leaching and application thereof
Lai et al. Deep eutectic solvent-mediated preparation of solvothermal carbon with rich carboxyl and phenol groups from crop straw for high-efficient uranium adsorption
CN111659453A (en) Visible light-ozone concerted catalysis catalyst and preparation method thereof
CN113058571B (en) Preparation method of bifunctional polymer adsorbent and application of bifunctional polymer adsorbent in gold recovery
CN103861564A (en) Preparation of graphene oxide adsorption material modified by dendritic polymer
CN112717892A (en) Copper-removing adsorbent for purifying cobalt-nickel electrolyte and preparation method thereof
CN105664864A (en) Preparation method and application of vascular plant based porous oxidative polymerization chelating adsorption material
Wang et al. Superior Au-adsorption performance of aminothiourea-modified waste cellulosic biomass
CN112076723A (en) Method for preparing heavy metal adsorbent by using Fenton sludge and application
CN114367267B (en) Mesoporous composite material and preparation method and application thereof
CN113088699B (en) Method for gold adsorption reduction recovery and strong acid recycling in waste circuit board pickle liquor
CN115948909A (en) Preparation method of super-hydrophilic carbon fiber
CN115155592A (en) Preparation method and application of iron cobaltate/coal gangue catalyst for efficiently activating persulfate
CN114632498B (en) Hyperbranched sulfydryl sponge adsorbent and preparation method and application thereof
CN114984928A (en) Modified porous cyclodextrin polymer material and preparation method and application thereof
CN109647410B (en) Preparation method of supported expanded graphite catalyst for treating EDTA-Cu wastewater
JP2011240287A (en) Solid chelating agent and method of manufacturing the same, and method for separation of cobalt, manganese and nickel employing the agent
CN113019342A (en) Preparation process of composite magnetic adsorbent, method for recovering germanium and application
CN112892486A (en) Preparation method of inorganic heavy metal waste liquid adsorption material, adsorption material and application
CN114762815A (en) Carbonate modified diatomite adsorbent and preparation method and application thereof
CN111644154A (en) Phosphorus removal material and preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant