WO2021052484A1 - Material for recovery of gold from waste water - Google Patents

Material for recovery of gold from waste water Download PDF

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Publication number
WO2021052484A1
WO2021052484A1 PCT/CN2020/116296 CN2020116296W WO2021052484A1 WO 2021052484 A1 WO2021052484 A1 WO 2021052484A1 CN 2020116296 W CN2020116296 W CN 2020116296W WO 2021052484 A1 WO2021052484 A1 WO 2021052484A1
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graphene
ions
gold
thiourea
zeolite
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PCT/CN2020/116296
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French (fr)
Chinese (zh)
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席行正
陈煜偈
陈廷钧
蔡政谚
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席行正
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    • 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
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • 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
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • 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
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • 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
    • 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
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/20Electrolytic production, recovery or refining of metals by electrolysis of solutions of noble metals
    • 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

Definitions

  • the invention relates to a thiourea graphene zeolite, and also relates to a preparation method of the thiourea graphene zeolite, in particular to the use of the thiourea graphene zeolite to absorb and desorb gold ions in a gold-containing solution.
  • the method of recovering gold from wastewater is mainly based on ion exchange resin as the adsorption material.
  • ion-exchange resin has no effect in the nitric acid system, and its lowest adsorption limit for gold ions is only 1 mg/L. Therefore, when the concentration of gold ions in the wastewater is lower than 1 mg/L, the absorption efficiency of the ion exchange resin for gold ions will be significantly worse.
  • the present invention provides a graphene composition and its use for the adsorption of gold.
  • the high selectivity of the graphene composition for gold ions is utilized, so that the use of the graphene composition for the adsorption of gold can have Lower adsorption limit, better adsorption efficiency and higher saturated adsorption capacity.
  • the present case provides a graphene composition, which comprises at least one compound of formula (I).
  • the nitrogen content of the aforementioned graphene composition is 2 to 4% by weight, and the sulfur content is 20 to 23% by weight.
  • the present application provides a method for using a graphene composition to adsorb a gold ion in a gold-containing solution, wherein the graphene composition includes at least one compound of the formula (I) structure.
  • the pH of the gold-containing solution in the above method is 2-6.
  • the graphene composition in the above method has an adsorption efficiency of 45% to 100% for the gold ions.
  • the saturated adsorption capacity of the gold ions per gram of the graphene composition in the above method is 810 to 850 mg.
  • the adsorption efficiency of the graphene composition on the lead ion is 1% To 2%, and the adsorption efficiency of the copper ions and the zinc ions is 0%.
  • the present application provides a method for processing a gold ion in a gold-containing solution, which comprises combining a graphene composition containing a compound of formula (I) with the gold ion in the gold-containing solution Steps of contact.
  • the above method further includes the step of desorbing the gold ions from the graphene composition containing the compound of formula (I) with a desorbent.
  • the desorption efficiency of gold ions in the above method is 90% to 96%.
  • the present case also provides a graphene composite, the graphene composite comprising a carrier, and a graphene composition comprising the structure compound of formula (I), the graphene composition is located on the carrier s surface.
  • the aforementioned carrier is a zeolite.
  • the carbon content on the surface of the aforementioned graphene composite is 49-52 weight.
  • the nitrogen content on the surface of the aforementioned graphene composite is 2 to 5% by weight.
  • the sulfur content on the surface of the aforementioned graphene composite is 3 to 6% by weight.
  • this case provides a method for manufacturing thiourea graphene zeolite, which includes the following steps: reacting a zeolite with a mixed solution containing 3-aminopropyltriethoxysilane and ethanol to obtain a reacted zeolite Mixing graphene oxide with water to form a suspension; dissolving thiourea in water to form a thiourea solution; and mixing and heating the thiourea solution, the suspension, and the reacted zeolite, To form a thiourea graphene zeolite.
  • the heating range in the above method is 75°C to 85°C.
  • the present application provides a method for adsorbing gold ions in a gold-containing solution using a graphene composite, the graphene composite comprising a carrier, and a graphene composition comprising a structure compound of formula (I)
  • the graphene composition is located on the surface of the carrier.
  • the pH of the gold-containing solution in the above method is 0-5.
  • the adsorption efficiency of the graphene zeolite for the gold ions in the above method is 60% to 100%.
  • the saturated adsorption capacity of the graphene zeolite for the gold ions per gram in the above method is 90 to 100 mg.
  • the adsorption efficiency of the thiourea graphene zeolite for the copper ions is 0.5 % To 5%
  • the adsorption efficiency for the lead ions is 2% to 5%
  • the adsorption efficiency for zinc ions is 0% to 5%
  • the adsorption efficiency for nickel ions is 0.5% to 5%.
  • FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention.
  • Figure 2A shows the analysis result of X-ray diffraction.
  • Figure 2B shows the analysis result of the scanning electron microscope.
  • Figure 2C shows the analysis result of a transmission electron microscope.
  • Figure 3A shows the effect of different reaction times on the adsorption efficiency of thiourea graphene.
  • Figure 3B shows the effect of different reaction pH values on the adsorption efficiency of thiourea graphene.
  • Figure 3C shows the effect of different doses of thiourea graphene on its adsorption efficiency.
  • Figure 3D shows the effect of different concentrations of ammonium thiosulfate solution on its desorption efficiency.
  • Figure 4 shows the isothermal adsorption curve of thiourea graphene for gold ions.
  • Figure 5A shows the adsorption efficiency of graphene oxide and graphene thiourea for gold ions, copper ions, lead ions, and zinc ions, respectively.
  • Figure 5B shows the selectivity and lowest adsorption limit of thiourea graphene for gold ions, copper ions, lead ions and zinc ions in wastewater.
  • Figure 5C shows the effect of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene.
  • Figure 6A shows the X-ray diffraction analysis result of thiourea graphene zeolite.
  • Figure 6B shows the scanning electron microscope analysis results of the thiourea graphene zeolite.
  • Figure 7 shows the effect of different reaction pH values on the adsorption efficiency of thiourea graphene zeolite.
  • Figure 8 shows the isotherm adsorption curve of thiourea graphene zeolite for gold ions.
  • Figure 9 shows the selectivity of thiourea graphene zeolite to gold ions, copper ions, lead ions, zinc ions, and nickel ions, respectively.
  • Example 1 Preparation and characterization of thiourea graphene and method for recovering gold
  • FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention.
  • step S110 to provide thiourea graphene.
  • the following steps are used to prepare thiourea graphene, but it is not limited thereto.
  • graphene oxide (GO) is mixed with ultrapure water to form a colloidal suspension of graphene oxide.
  • the thiourea solution was added to the colloidal suspension of graphene oxide, and stirred with a magnetic stir bar at 95°C for 8 hours to form thiourea graphene (TU-rGO), the chemical structure of which is as follows: (I) shown.
  • the TU-rGO solution was washed with ultrapure water and filtered to obtain thiourea graphene solids.
  • the solid was dried at 50°C for 24 hours, and then the thiourea graphene solid was ground with an agate mortar. Then, pass through a 30-mesh sieve and a 60-mesh sieve in sequence to obtain thiourea graphene with a particle size between 0.25 mm and 0.59 mm.
  • step S120 is performed to add thiourea graphene to the wastewater to perform an adsorption reaction.
  • the wastewater includes at least gold ions.
  • the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50 ml. And the reaction time is 12, 24, 48, 72, 96, 120 hours, respectively.
  • Adsorption efficiency (%) (C0-Ct)/C0 ⁇ 100%, where C0 is the concentration of gold ions before the adsorption reaction (mg/L), and Ct is the concentration of gold ions after the adsorption reaction (mg/L) .
  • Example 3 The effect of pH value of reaction on adsorption efficiency
  • the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the reaction time is 96 hours, and the reaction volume is 50 ml. , And the pH values of the reaction are 2, 3, 4, 5, 6, 7, 8, 9, 10 respectively.
  • Example 4 The effect of the dosage of thiourea graphene on the adsorption efficiency
  • the reaction conditions are: the concentration of gold ions is 10 mg/liter, the reaction temperature is 30° C., the oscillation speed is 150 rpm, the reaction time is 96 hours, the reaction volume is 50 ml, the pH value is 5, and the sulfur
  • the dosages of urea graphene are 0.5, 1.0, 1.5, and 2.0 mg, respectively.
  • step S130 is performed to separate the thiourea graphene adsorbing gold ions from the wastewater.
  • the thiourea graphene adsorbs the gold ions in the wastewater, for example, it is filtered with a Syringe filter with a pore size of 0.45 microns, so that the reacted thiourea graphene cannot pass through.
  • the pores further separate the thiourea graphene that adsorbs gold ions from the wastewater after the reaction.
  • the gold ion concentration in the separated wastewater is measured with an inductively coupled plasma emission spectrometer (ICP-OES), and used as the gold ion concentration after the reaction in Formula 1.
  • ICP-OES inductively coupled plasma emission spectrometer
  • step S140 is performed to perform a desorption reaction on the thiourea graphene adsorbing gold ions to obtain gold ions.
  • a desorbent is added to the thiourea graphene separated from the wastewater after the reaction and adsorbed with gold ions, so that the gold ions can be desorbed from the thiourea graphene.
  • the desorption agent is, for example, ammonium thiosulfate, but it is not limited to this.
  • Example 5 Influence of concentration of ammonium thiosulfate solution on desorption efficiency
  • the ammonium thiosulfate solution is divided into three groups A, B, and C according to the concentration of the ammonium thiosulfate solution used, and each group undergoes two desorption reactions.
  • each group adds 0.2M ammonium thiosulfate solution to 2.0 mg of thiourea graphene with gold ions adsorbed (the content of gold ions adsorbed per gram of thiourea graphene is 2500 mg) to perform the first Second desorption reaction.
  • the three groups A, B, and C are respectively used for the second desorption reaction with 0.05, 0.1 or 0.2M ammonium thiosulfate solution.
  • the first desorption reaction and the second desorption reaction are carried out according to the following reaction conditions: the reaction temperature is 30°C, the shaking speed is 150 rpm, the reaction time is 24 hours, the reaction volume is 50 ml, and the pH value of the reaction Respectively 7.4.
  • the first desorption reaction can desorb most of the gold ions from the thiourea graphene, and the desorption efficiency is about 93% or more.
  • 0.2M ammonium thiosulfate solution (group C) can increase the desorption efficiency by about 1.4%. That is to say, the desorption reaction with ammonium thiosulfate solution can make the desorption efficiency of gold ions on the thiourea graphene be 93% to 96%.
  • the desorption efficiency is calculated according to Formula 2.
  • the concentration of gold ions in the wastewater in the real environment may be lower than 10 mg/L, and may also contain other metal ions, such as copper. Ions, lead ions, zinc ions, or combinations thereof. Therefore, in the following, different examples will be used to discuss the minimum adsorbable concentration of thiourea graphene for gold ions, and to discuss the selectivity of thiourea graphene for gold ions and other metal ions.
  • Example 6 Comparison of graphene oxide and graphene thiourea, respectively, the adsorption efficiency of gold ions, copper ions, lead ions and zinc ions
  • 2.0 mg of graphene oxide (or 2.0 mg of thiourea graphene) is used with gold ions (labeled as Au) at a concentration of 10 mg/L and copper ions at a concentration of 20 mg/L
  • Au gold ions
  • the adsorption reaction is carried out with lead ions with a concentration of 20 mg/L (labeled as Pb), and zinc ions with a concentration of 20 mg/L (labeled as Zn)
  • the reaction conditions are: reaction temperature of 30°C, The shaking speed is 150 rpm, the pH value is 2, the reaction volume is 50 ml, and the reaction time is 96 hours.
  • Example 7 Selectivity of thiourea graphene to gold ions, copper ions, lead ions and zinc ions in wastewater
  • the wastewater is divided into experimental example 1, experimental example 2, and experimental example 3 according to the composition and content of the wastewater.
  • the wastewater of Experimental Example 1 includes gold ions with a concentration of 10 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 2 includes gold ions with a concentration of 1 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 3 includes gold ions with a concentration of 0.1 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 4 includes gold ions with a concentration of 0.01 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the reaction conditions of Experimental Example 1, Experimental Example 2, Experimental Example 3, and Experimental Example 4 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50. The reaction time is 96 hours.
  • the adsorption efficiency of thiourea graphene for gold ions is 98.3 ⁇ 0.8%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions.
  • the adsorption efficiency of thiourea graphene for gold ions is 98.9 ⁇ 0.3%, and the adsorption efficiency for lead ions is about 1% to 2%, but it has no adsorption efficiency for copper ions and zinc ions.
  • the adsorption efficiency of thiourea graphene for gold ions is 100%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions.
  • the lowest adsorbable concentration (lowest adsorption limit) of thiourea graphene for gold ions is 0.01 mg/L.
  • the gold ion is 0.01 mg/L to 10 mg/L, the thiourea graphene has high selectivity for gold ions and an adsorption efficiency of more than 98%.
  • Example 8 The effect of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene
  • the wastewater is divided into experimental example 5, experimental example 6, experimental example 7, and experimental example 8 according to the composition and content of the wastewater.
  • the wastewater of Experimental Example 5 includes gold ions with a concentration of 10 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 6 includes gold ions with a concentration of 1 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 7 includes gold ions with a concentration of 0.1 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the wastewater of Experimental Example 8 includes gold ions with a concentration of 0.01 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L.
  • the reaction conditions of experimental example 5, experimental example 6, experimental example 7 and experimental example 8 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50.
  • the reaction time is 96 hours.
  • the thiourea graphene in Experimental Example 8 has an adsorption efficiency of 100% for gold ions and an adsorption efficiency of about 5% for lead ions, but it still has no effect on copper ions and zinc ions. Adsorption efficiency. Therefore, even if the concentration of copper ions in the wastewater is increased, graphene thiourea still has high selectivity for gold ions and an adsorption efficiency of 95% to 100%.
  • the following steps are used to prepare the thiourea graphene zeolite, but it is not limited thereto.
  • graphene oxide is mixed with ultrapure water to form a colloidal suspension of graphene oxide, and thiourea is dissolved in ultrapure water to form a thiourea solution.
  • thiourea solution was added to the colloidal suspension of graphene oxide to form a thiourea-graphene mixed solution, and then put into the organically modified zeolite, reacted at 80°C for 4 hours, and finally the solid was dried at 50°C for 24 hours After hours, thiourea graphene zeolite was obtained.
  • thiourea graphene zeolite is black, and it is composed of multiple unit elements including zeolite, graphene and thiourea.
  • graphene is a kind of hexagonal honeycomb lattice composed of carbon atoms and sp2 hybrid orbitals.
  • a flat film a two-dimensional material with the thickness of only one carbon atom.
  • the appearance presents a highly folded three-dimensional ridgeline structure. It is composed of graphene sheets with a radial size of 2-6 ⁇ m, and the graphene sheets cross each other.
  • the connection forms a macroporous structure with a size of 50 nm or more.
  • thiourea graphene zeolite The structure of thiourea graphene zeolite is based on zeolite, and the outer surface of the zeolite is covered by thiourea graphene composed of graphene and thiourea.
  • the chemical structure of thiourea graphene is shown in formula (I).
  • Example 10 The influence of the pH value of the reaction on the adsorption efficiency of thiourea graphene zeolite
  • the test conditions are: 0.01 g of thiourea graphene zeolite, a gold ion concentration of 10 ml/liter, a reaction temperature of 30°C, an oscillation speed of 150 rpm, a reaction time of 24 hours, and a reaction volume of 50 ml , And the pH of the reaction is 0, 1, 2, 3, 4, 5, 6, 7, 8, 9 and 10, respectively.
  • Example 11 Determination of the saturated adsorption capacity of thiourea graphene zeolite for gold ions
  • thiourea graphene zeolite was used to perform adsorption experiments in solutions of different gold ion concentrations, and the obtained experimental data was applied to Langmuir adsorption
  • a simulation of the adsorption isotherm curve is performed, and the result is shown in Figure 8. It can be seen from the simulation results in Fig. 8 that the correlation coefficient R2 of the adsorption isotherm curve is 0.97, and the saturated adsorption capacity of gold ions per gram of thiourea graphene zeolite is 97.1 mg.
  • Example 12 Selectivity of thiourea graphene zeolite to gold ions, copper ions, lead ions and zinc ions in wastewater
  • the wastewater of Experimental Example 1 includes gold ions with a concentration of 1 ml/liter, copper ions with a concentration of 100 ml/liter, and lead with a concentration of 20 ml/liter. Ions, zinc ions with a concentration of 20 ml/liter, nickel ions with a concentration of 20 ml/liter.
  • the wastewater of Example 2 includes gold ions with a concentration of 10 ml/liter, copper ions with a concentration of 100 ml/liter, lead ions with a concentration of 20 ml/liter, zinc ions with a concentration of 20 ml/liter, and a concentration of 20 ml. /L of nickel ion.
  • the reaction conditions of Experimental Example 1 and Experimental Example 2 are: 0.01 g of thiourea graphene zeolite, reaction temperature of 30° C., oscillation speed of 150 rpm, reaction time of 24 hours, and reaction volume of 50 ml.
  • the adsorption efficiency of thiourea graphene zeolite for gold ions is about 93.13%, and the adsorption efficiency for copper ions, lead ions, zinc ions, and nickel ions are all less than 5%.
  • the adsorption efficiency of thiourea graphene zeolite for gold ions was 94.05%, and the adsorption efficiency for copper ions, lead ions, zinc ions, and nickel ions were 0.86%, 2.73%, 4.36%, and 0.81%, respectively. Therefore, thiourea graphene zeolite has high selectivity for gold ions and an adsorption efficiency of 93% to 94%.
  • the high selectivity of thiourea graphene zeolite for gold ions makes the use of thiourea graphene zeolite to When the gold ion in the gold-containing solution undergoes an adsorption reaction, it can have a lower adsorption limit, a better adsorption efficiency, and a higher saturated adsorption capacity.

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Abstract

A graphene composite comprises a carrier and a graphene composition comprising a structural compound expressed in formula (I). The graphene composition is positioned on a surface of the carrier. Also disclosed are a method of preparing a thiourea-graphene-zeolite material, and a method employing the above graphene composition/composite to adsorb gold ions in a gold-containing solution.

Description

一种回收含金废水之材料A material for recycling gold-containing wastewater
本申请要求于2019年9月20日提交的CN201910895143.6的优先权,上述在先申请的内容以引入的方式并入本文本中。This application claims the priority of CN201910895143.6 filed on September 20, 2019, and the content of the above-mentioned earlier application is incorporated into this text by way of introduction.
技术领域Technical field
本发明涉及一种硫脲石墨烯沸石,也涉及了一种硫脲石墨烯沸石的制备方法,尤其涉及一种使用硫脲石墨烯沸石于一含金溶液中吸脱附金离子的用途。The invention relates to a thiourea graphene zeolite, and also relates to a preparation method of the thiourea graphene zeolite, in particular to the use of the thiourea graphene zeolite to absorb and desorb gold ions in a gold-containing solution.
背景技术Background technique
目前,从废水中回收金的方法,是以离子交换树脂作为吸附材的方法为主,其相较于传统的电解法,较能符合环保节能的趋势,且同时具有良好的吸附效率以及回收率。然而,离子交换树脂在硝酸体系中却无法产生作用,且其对于金离子的最低吸附极限只有1毫克/升。因此,当废水中的金离子浓度低于1毫克/升时,离子交换树脂对于金离子的吸效附效率则会明显变差。At present, the method of recovering gold from wastewater is mainly based on ion exchange resin as the adsorption material. Compared with the traditional electrolysis method, it is more in line with the trend of environmental protection and energy saving, and at the same time has good adsorption efficiency and recovery rate. . However, ion-exchange resin has no effect in the nitric acid system, and its lowest adsorption limit for gold ions is only 1 mg/L. Therefore, when the concentration of gold ions in the wastewater is lower than 1 mg/L, the absorption efficiency of the ion exchange resin for gold ions will be significantly worse.
发明内容Summary of the invention
本发明提供一种使用石墨烯组合物及其用于吸附金的用途,利用所述石墨烯组合物对于金离子的高选择性,使得使用所述石墨烯组合物用于吸附金的用途可具有较低的吸附极限、较佳的吸附效率以及较高的饱和吸附容量。The present invention provides a graphene composition and its use for the adsorption of gold. The high selectivity of the graphene composition for gold ions is utilized, so that the use of the graphene composition for the adsorption of gold can have Lower adsorption limit, better adsorption efficiency and higher saturated adsorption capacity.
在一方面,本案提供一种石墨烯组合物,所述石墨烯组合物至少包含一式(I)结构的化合物。In one aspect, the present case provides a graphene composition, which comprises at least one compound of formula (I).
Figure PCTCN2020116296-appb-000001
Figure PCTCN2020116296-appb-000001
在一实施例中,上述的石墨烯组合物的氮含量为2~4重量%,且硫含量为20~23重量%。In one embodiment, the nitrogen content of the aforementioned graphene composition is 2 to 4% by weight, and the sulfur content is 20 to 23% by weight.
在另一方面,本案提供一种使用一石墨烯组合物于一含金溶液中吸附一金离子的方法,其特征在于,所述石墨烯组合物至少包含一式(I)结构的化合物。In another aspect, the present application provides a method for using a graphene composition to adsorb a gold ion in a gold-containing solution, wherein the graphene composition includes at least one compound of the formula (I) structure.
Figure PCTCN2020116296-appb-000002
Figure PCTCN2020116296-appb-000002
在一实施例中,上述方法中的含金溶液的pH值为2至6。In one embodiment, the pH of the gold-containing solution in the above method is 2-6.
在一实施例中,上述方法中的石墨烯组合物对所述金离子的吸附效率为45%至100%。In one embodiment, the graphene composition in the above method has an adsorption efficiency of 45% to 100% for the gold ions.
在一实施例中,上述方法中的每克所述石墨烯组合物对所述金离子的饱和吸附容量为810至850毫克。In an embodiment, the saturated adsorption capacity of the gold ions per gram of the graphene composition in the above method is 810 to 850 mg.
在一实施例中,上述方法中当所述含金溶液还包括一铜离子、一铅离子、一锌离子或其 组合时,所述石墨烯组合物对所述铅离子的吸附效率为1%至2%,且对所述铜离子及所述锌离子的吸附效率为0%。In one embodiment, in the above method, when the gold-containing solution further includes a copper ion, a lead ion, a zinc ion or a combination thereof, the adsorption efficiency of the graphene composition on the lead ion is 1% To 2%, and the adsorption efficiency of the copper ions and the zinc ions is 0%.
在另一方面,本案提供一种于一含金溶液中处理一金离子的方法,其包含将一包含式(I)结构化合物的石墨烯组合物与所述含金溶液中之所述金离子接触的步骤。In another aspect, the present application provides a method for processing a gold ion in a gold-containing solution, which comprises combining a graphene composition containing a compound of formula (I) with the gold ion in the gold-containing solution Steps of contact.
Figure PCTCN2020116296-appb-000003
Figure PCTCN2020116296-appb-000003
在一实施例中,上述方法中还包含以一脱附剂使所述金离子从所述包含式(I)化合物的石墨烯组合物上脱附的步骤。In one embodiment, the above method further includes the step of desorbing the gold ions from the graphene composition containing the compound of formula (I) with a desorbent.
在一实施例中,上述方法中的金离子的脱附效率为90%至96%。In one embodiment, the desorption efficiency of gold ions in the above method is 90% to 96%.
在另一方面,本案还提供一种石墨烯复合物,所述石墨烯复合物包含一载体,以及一包含式(I)结构化合物的石墨烯组合物,所述石墨烯组合物位于所述载体的表面。In another aspect, the present case also provides a graphene composite, the graphene composite comprising a carrier, and a graphene composition comprising the structure compound of formula (I), the graphene composition is located on the carrier s surface.
Figure PCTCN2020116296-appb-000004
Figure PCTCN2020116296-appb-000004
在一实施例中,上述的所述载体为一沸石。In one embodiment, the aforementioned carrier is a zeolite.
在一实施例中,上述的石墨烯复合物经X光衍射于2θ=12.46o及23.68o具有明显的衍射峰。In one embodiment, the above-mentioned graphene composite has obvious diffraction peaks after X-ray diffraction at 2θ=12.46° and 23.68°.
在一实施例中,上述的石墨烯复合物表面的碳含量为49~52重量。In one embodiment, the carbon content on the surface of the aforementioned graphene composite is 49-52 weight.
在一实施例中,上述的石墨烯复合物表面的氮含量为2~5重量%。In one embodiment, the nitrogen content on the surface of the aforementioned graphene composite is 2 to 5% by weight.
在一实施例中,上述的石墨烯复合物表面的硫含量为3~6重量%。In one embodiment, the sulfur content on the surface of the aforementioned graphene composite is 3 to 6% by weight.
在另一方面,本案提供一种制造硫脲石墨烯沸石的方法,其包括以下步骤:将一沸石与一含3-氨基丙基三乙氧基硅烷及乙醇混和溶液反应,得到一反应后沸石;将氧化石墨烯与水混合以形成一悬浮液;将硫脲溶解在水中以形成一硫脲溶液;以及将所述硫脲溶液、所述悬浮液与所述反应后沸石相混和并加热,以形成一硫脲石墨烯沸石。In another aspect, this case provides a method for manufacturing thiourea graphene zeolite, which includes the following steps: reacting a zeolite with a mixed solution containing 3-aminopropyltriethoxysilane and ethanol to obtain a reacted zeolite Mixing graphene oxide with water to form a suspension; dissolving thiourea in water to form a thiourea solution; and mixing and heating the thiourea solution, the suspension, and the reacted zeolite, To form a thiourea graphene zeolite.
在一实施例中,上述方法中的加热范围为75℃至85℃。In one embodiment, the heating range in the above method is 75°C to 85°C.
在另一方面,本案提供一种使用一石墨烯复合物于一含金溶液中吸附金离子的方法,所述石墨烯复合物包含一载体,以及一包含式(I)结构化合物的石墨烯组合物,所述石墨烯组合物位于所述载体的表面。In another aspect, the present application provides a method for adsorbing gold ions in a gold-containing solution using a graphene composite, the graphene composite comprising a carrier, and a graphene composition comprising a structure compound of formula (I) The graphene composition is located on the surface of the carrier.
Figure PCTCN2020116296-appb-000005
Figure PCTCN2020116296-appb-000005
在一实施例中,上述方法中的所述含金溶液的pH值为0至5。In one embodiment, the pH of the gold-containing solution in the above method is 0-5.
在一实施例中,上述方法中的所述石墨烯沸石对所述金离子的吸附效率为60%至100%。In one embodiment, the adsorption efficiency of the graphene zeolite for the gold ions in the above method is 60% to 100%.
在一实施例中,上述方法中的每克所述石墨烯沸石对所述金离子的饱和吸附容量为90至100毫克。In one embodiment, the saturated adsorption capacity of the graphene zeolite for the gold ions per gram in the above method is 90 to 100 mg.
在一实施例中,上述方法中当所述含金溶液还包括铜离子、铅离子、锌离子、镍离子或其组合时,所述硫脲石墨烯沸石对所述铜离子的吸附效率为0.5%至5%,对所述铅离子的吸附效率为2%至5%,对锌离子的吸附效率为0%至5%,以及对镍离子的吸附效率为0.5%至5%。In one embodiment, in the above method, when the gold-containing solution further includes copper ions, lead ions, zinc ions, nickel ions, or a combination thereof, the adsorption efficiency of the thiourea graphene zeolite for the copper ions is 0.5 % To 5%, the adsorption efficiency for the lead ions is 2% to 5%, the adsorption efficiency for zinc ions is 0% to 5%, and the adsorption efficiency for nickel ions is 0.5% to 5%.
为让本发明的上述特征和优点能更明显易懂,下文特举实施例,并配合附图作详细说明如下。In order to make the above-mentioned features and advantages of the present invention more comprehensible, the following specific embodiments are described in detail in conjunction with the accompanying drawings.
附图说明Description of the drawings
图1示出为本发明一实施例的一种硫脲石墨烯的回收金的方法的流程图。FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention.
图2A为X光衍射的分析结果。Figure 2A shows the analysis result of X-ray diffraction.
图2B为扫描式电子显微镜的分析结果。Figure 2B shows the analysis result of the scanning electron microscope.
图2C为穿透式电子显微镜的分析结果。Figure 2C shows the analysis result of a transmission electron microscope.
图3A为不同的反应时间对硫脲石墨烯的吸附效率的影响。Figure 3A shows the effect of different reaction times on the adsorption efficiency of thiourea graphene.
图3B为不同的反应的pH值对硫脲石墨烯的吸附效率的影响。Figure 3B shows the effect of different reaction pH values on the adsorption efficiency of thiourea graphene.
图3C为不同剂量的硫脲石墨烯对其吸附效率的影响。Figure 3C shows the effect of different doses of thiourea graphene on its adsorption efficiency.
图3D为不同浓度的硫代硫酸铵溶液对其脱附效率的影响。Figure 3D shows the effect of different concentrations of ammonium thiosulfate solution on its desorption efficiency.
图4为硫脲石墨烯对金离子的等温吸附曲线。Figure 4 shows the isothermal adsorption curve of thiourea graphene for gold ions.
图5A为氧化石墨烯及硫脲石墨烯分别对金离子、铜离子、铅离子及锌离子的吸附效率。Figure 5A shows the adsorption efficiency of graphene oxide and graphene thiourea for gold ions, copper ions, lead ions, and zinc ions, respectively.
图5B为硫脲石墨烯对废水中的金离子、铜离子、铅离子及锌离子的选择性以及最低吸附极限。Figure 5B shows the selectivity and lowest adsorption limit of thiourea graphene for gold ions, copper ions, lead ions and zinc ions in wastewater.
图5C为废水中的铜离子浓度对硫脲石墨烯的吸附效率的影响。Figure 5C shows the effect of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene.
图6A为硫脲石墨烯沸石X光衍射分析结果。Figure 6A shows the X-ray diffraction analysis result of thiourea graphene zeolite.
图6B为硫脲石墨烯沸石扫描式电子显微镜的分析结果。Figure 6B shows the scanning electron microscope analysis results of the thiourea graphene zeolite.
图7为不同的反应pH值对硫脲石墨烯沸石的吸附效率的影响。Figure 7 shows the effect of different reaction pH values on the adsorption efficiency of thiourea graphene zeolite.
图8为硫脲石墨烯沸石对金离子的等温吸附曲线。Figure 8 shows the isotherm adsorption curve of thiourea graphene zeolite for gold ions.
图9为硫脲石墨烯沸石分別对金离子、铜离子、铅离子、锌离子及镍离子的选择性。Figure 9 shows the selectivity of thiourea graphene zeolite to gold ions, copper ions, lead ions, zinc ions, and nickel ions, respectively.
附图标记说明Description of Reference Signs
S110、S120、S130、S140:步骤S110, S120, S130, S140: steps
具体实施方式detailed description
实施例1:硫脲石墨烯的制备、定性以及用于回收金的方法Example 1: Preparation and characterization of thiourea graphene and method for recovering gold
图1示出为本发明一实施例的一种硫脲石墨烯的回收金的方法的流程图。FIG. 1 shows a flowchart of a method for recovering gold from thiourea graphene according to an embodiment of the present invention.
请参照图1,进行步骤S110,提供硫脲石墨烯。在本实施例中,例如是以以下步骤来制备硫脲石墨烯,但不以此为限。首先,将氧化石墨烯(graphene oxide,GO)与超纯水(ultrapure water)混合以形成氧化石墨烯的胶体悬浮液。将硫脲溶解在超纯水中,以形成硫脲溶液。然后,将硫脲溶液加入于氧化石墨烯的胶体悬浮液中,以磁力搅拌棒在95℃下进行搅拌8小时,以形成硫脲石墨烯(thiourea graphene,TU-rGO),其化学结构式如式(I)所示。Please refer to FIG. 1 to perform step S110 to provide thiourea graphene. In this embodiment, for example, the following steps are used to prepare thiourea graphene, but it is not limited thereto. First, graphene oxide (GO) is mixed with ultrapure water to form a colloidal suspension of graphene oxide. Dissolve thiourea in ultrapure water to form a thiourea solution. Then, the thiourea solution was added to the colloidal suspension of graphene oxide, and stirred with a magnetic stir bar at 95°C for 8 hours to form thiourea graphene (TU-rGO), the chemical structure of which is as follows: (I) shown.
随后,用超纯水洗涤TU-rGO溶液并过滤,以获得硫脲石墨烯固体。最后,再将固体于50℃下干燥24小时后,以玛瑙研钵对硫脲石墨烯固体进行研磨。接着,依序通过30目筛(mesh sieve)以及60目筛,以获得粒径在0.25毫米至0.59毫米之间的硫脲石墨烯。Subsequently, the TU-rGO solution was washed with ultrapure water and filtered to obtain thiourea graphene solids. Finally, the solid was dried at 50°C for 24 hours, and then the thiourea graphene solid was ground with an agate mortar. Then, pass through a 30-mesh sieve and a 60-mesh sieve in sequence to obtain thiourea graphene with a particle size between 0.25 mm and 0.59 mm.
Figure PCTCN2020116296-appb-000006
Figure PCTCN2020116296-appb-000006
接着,对氧化石墨烯以及硫脲石墨烯中的元素成份及其含量进行分析,其结果如表1所示。Next, the element components and contents in graphene oxide and graphene thiourea were analyzed, and the results are shown in Table 1.
表1Table 1
 To C(%)C(%) O(%)O(%) H(%)H(%) N(%)N(%) S(%)S(%)
GOGO 47.21±0.0147.21±0.01 39.99±1.7039.99±1.70 2.75±0.082.75±0.08 0.13±0.020.13±0.02 3.72±0.003.72±0.00
TU-rGOTU-rGO 60.38±1.2260.38±1.22 10.00±0.0810.00±0.08 1.05±0.101.05±0.10 2.01±0.222.01±0.22 22.87±0.3422.87±0.34
由表1的结果可知,相较于氧化石墨烯,硫脲石墨烯的氮含量及硫含量分别增加至2.01%以及22.87%,且氧含量减少至10.00%。表示硫脲石墨烯是通过取代氧的方式来增加氮、硫的含量。From the results in Table 1, it can be seen that compared to graphene oxide, the nitrogen content and sulfur content of graphene thiourea are increased to 2.01% and 22.87%, respectively, and the oxygen content is reduced to 10.00%. It means that graphene thiourea increases the content of nitrogen and sulfur by substituting oxygen.
接着,由图2A的X光衍射的分析结果可知,相较于石墨烯的衍射峰位置(2θ=26.5°)以及氧化石墨烯的衍射峰位置(2θ=26.5°或10.5°),硫脲石墨烯具有的衍射峰位置为2θ=23.05°。Next, from the X-ray diffraction analysis results of Figure 2A, it can be seen that compared with the diffraction peak position of graphene (2θ=26.5°) and the diffraction peak position of graphene oxide (2θ=26.5° or 10.5°), thiourea graphite The diffraction peak position of alkene is 2θ=23.05°.
由图2B的扫描式电子显微镜的分析结果可知,在3000倍的放大图中,硫脲石墨烯的表面具有高度折叠的结构。由图2C的穿透式电子显微镜的分析结果可知,在60000倍的放大图中,硫脲石墨烯具有多层结构,且测得的比表面积为4.5m2/g。From the analysis result of the scanning electron microscope in FIG. 2B, it can be seen that the surface of the graphene thiourea has a highly folded structure in a magnified view of 3000 times. From the analysis result of the transmission electron microscope in FIG. 2C, it can be seen that in the 60,000 times magnification, the thiourea graphene has a multilayer structure, and the measured specific surface area is 4.5 m2/g.
接着,进行步骤S120,将硫脲石墨烯加入至废水中,以进行吸附反应。在本实施例中,废水至少包括金离子。Then, step S120 is performed to add thiourea graphene to the wastewater to perform an adsorption reaction. In this embodiment, the wastewater includes at least gold ions.
以下将以不同的实施例来探讨硫脲石墨烯对废水中的金离子进行吸附反应的反应条件。In the following, different examples will be used to explore the reaction conditions for the adsorption reaction of thiourea graphene to gold ions in the wastewater.
实施例2:反应时间对吸附效率的影响Example 2: Effect of reaction time on adsorption efficiency
在本实施例中,反应条件为:硫脲石墨烯为0.5毫克、金离子的浓度为10毫克/升、反应温度为30℃、振荡速度为150rpm、pH值为2、反应体积为50毫升,且反应时间分别为12、24、48、72、96、120小时。In this embodiment, the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50 ml. And the reaction time is 12, 24, 48, 72, 96, 120 hours, respectively.
由图3A的结果可知,当反应时间为96小时,硫脲石墨烯对金离子的吸附效率约为82.7±6.1%。当反应时间为120小时,硫脲石墨烯对金离子的吸附效率则没有显著地增加。也就是说,当反应时间为96小时,硫脲石墨烯对金离子的吸附动力学可达到一平衡,且可以展现不错的吸附效率。It can be seen from the result of FIG. 3A that when the reaction time is 96 hours, the adsorption efficiency of thiourea graphene for gold ions is about 82.7±6.1%. When the reaction time is 120 hours, the adsorption efficiency of thiourea graphene for gold ions does not increase significantly. That is to say, when the reaction time is 96 hours, the adsorption kinetics of thiourea graphene to gold ions can reach an equilibrium, and can exhibit good adsorption efficiency.
须要说明的是,在本实施例中,吸附效率是依据公式1来计算。公式1:吸附效率(%)=(C0-Ct)/C0×100%,其中C0为吸附反应前的金离子浓度(毫克/升),Ct为吸附反应后的金离子浓度(毫克/升)。It should be noted that in this embodiment, the adsorption efficiency is calculated according to Formula 1. Formula 1: Adsorption efficiency (%) = (C0-Ct)/C0×100%, where C0 is the concentration of gold ions before the adsorption reaction (mg/L), and Ct is the concentration of gold ions after the adsorption reaction (mg/L) .
实施例3:反应的pH值对吸附效率的影响Example 3: The effect of pH value of reaction on adsorption efficiency
在本实施例中,反应条件为:硫脲石墨烯为0.5毫克、金离子的浓度为10毫克/升、反应温度为30℃、振荡速度为150rpm、反应时间为96小时、反应体积为50毫升,且反应的pH值分别为2、3、4、5、6、7、8、9、10。In this embodiment, the reaction conditions are: graphene thiourea is 0.5 mg, the concentration of gold ions is 10 mg/liter, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the reaction time is 96 hours, and the reaction volume is 50 ml. , And the pH values of the reaction are 2, 3, 4, 5, 6, 7, 8, 9, 10 respectively.
由图3B的结果可知,当反应的pH值为2~5时,硫脲石墨烯对金离子的吸附效率约为80~85%。当反应的pH值为6时,硫脲石墨烯对金离子的吸附效率约为40~50%。然而,当 反应的pH值超过6时,硫脲石墨烯对金离子的吸附效率则快速地降低至20%以下。也就是说,当反应的pH值为2~5时,硫脲石墨烯对金离子都可以展现不错的吸附效率。It can be seen from the result of FIG. 3B that when the pH of the reaction is 2-5, the adsorption efficiency of thiourea graphene for gold ions is about 80-85%. When the pH of the reaction is 6, the adsorption efficiency of thiourea graphene for gold ions is about 40-50%. However, when the pH of the reaction exceeds 6, the adsorption efficiency of thiourea graphene for gold ions quickly drops below 20%. In other words, when the pH of the reaction is 2 to 5, graphene thiourea can exhibit good adsorption efficiency for gold ions.
实施例4:硫脲石墨烯的剂量对吸附效率的影响Example 4: The effect of the dosage of thiourea graphene on the adsorption efficiency
在本实施例中,反应条件为:金离子的浓度为10毫克/升、反应温度为30℃、振荡速度为150rpm、反应时间为96小时、反应体积为50毫升、pH值为5,且硫脲石墨烯的剂量分别为0.5、1.0、1.5、2.0毫克。In this embodiment, the reaction conditions are: the concentration of gold ions is 10 mg/liter, the reaction temperature is 30° C., the oscillation speed is 150 rpm, the reaction time is 96 hours, the reaction volume is 50 ml, the pH value is 5, and the sulfur The dosages of urea graphene are 0.5, 1.0, 1.5, and 2.0 mg, respectively.
由图3C的结果可知,当硫脲石墨烯的剂量为0.5毫克时,硫脲石墨烯对金离子的吸附效率约为82.7±6.1%。然而,当硫脲石墨烯的剂量为1.0、1.5或2.0毫克时,硫脲石墨烯对金离子的吸附效率只有些微地增加。也就是说,当硫脲石墨烯的剂量为0.5~2.0毫克时,其对金离子都可以展现不错的吸附效率。It can be seen from the result of FIG. 3C that when the dose of thiourea graphene is 0.5 mg, the adsorption efficiency of thiourea graphene for gold ions is about 82.7±6.1%. However, when the dose of thiourea graphene is 1.0, 1.5, or 2.0 mg, the adsorption efficiency of thiourea graphene for gold ions only slightly increases. In other words, when the dosage of thiourea graphene is 0.5-2.0 mg, it can exhibit good adsorption efficiency for gold ions.
然后,进行步骤S130,将吸附金离子的硫脲石墨烯与废水分离。在本实施例中,在硫脲石墨烯吸附废水中的金离子之后,例如是以孔洞大小为0.45微米的针筒过滤器(Syringe filter)进行过滤,以使反应后的硫脲石墨烯无法通过孔洞,进而将吸附金离子的硫脲石墨烯与反应后的废水分离。接着,以感应耦合等离子体放射光谱仪(Inductively Couple Plasma Optical Emission Spectrometry,ICP-OES)测量分离后的废水中的金离子浓度,以作为公式1中的反应后的金离子浓度。Then, step S130 is performed to separate the thiourea graphene adsorbing gold ions from the wastewater. In this embodiment, after the thiourea graphene adsorbs the gold ions in the wastewater, for example, it is filtered with a Syringe filter with a pore size of 0.45 microns, so that the reacted thiourea graphene cannot pass through. The pores further separate the thiourea graphene that adsorbs gold ions from the wastewater after the reaction. Next, the gold ion concentration in the separated wastewater is measured with an inductively coupled plasma emission spectrometer (ICP-OES), and used as the gold ion concentration after the reaction in Formula 1.
最后,进行步骤S140,对吸附金离子的硫脲石墨烯进行脱附反应,以得到金离子。在本实施例中,例如是将脱附剂加入于上述与反应后的废水分离且吸附有金离子的硫脲石墨烯中,以使金离子可从硫脲石墨烯上脱附。在本实施例中,脱附剂例如是硫代硫酸铵(ammonium thiosulfate),但不以此为限。Finally, step S140 is performed to perform a desorption reaction on the thiourea graphene adsorbing gold ions to obtain gold ions. In this embodiment, for example, a desorbent is added to the thiourea graphene separated from the wastewater after the reaction and adsorbed with gold ions, so that the gold ions can be desorbed from the thiourea graphene. In this embodiment, the desorption agent is, for example, ammonium thiosulfate, but it is not limited to this.
以下将以不同的实施例来探讨硫代硫酸铵对吸附有金离子的硫脲石墨烯进行脱附反应的反应条件。In the following, different examples will be used to discuss the reaction conditions of the desorption reaction of ammonium thiosulfate on thiourea graphene adsorbed with gold ions.
实施例5:硫代硫酸铵溶液的浓度对脱附效率的影响Example 5: Influence of concentration of ammonium thiosulfate solution on desorption efficiency
在本实施例中,依据所使用的硫代硫酸铵溶液的浓度分为A、B、C三组,且每组皆进行两次脱附反应。首先,每组皆在2.0毫克吸附有金离子的硫脲石墨烯(每克硫脲石墨烯所吸附的金离子的含量为2500毫克)中加入0.2M的硫代硫酸铵溶液,以进行第一次脱附反应。接着,在进行完第一次脱附反应之后,A、B、C三组分别以0.05、0.1或0.2M的硫代硫酸铵溶液进行第二次脱附反应。此外,第一次脱附反应与第二次脱附反应皆依据以下的反应条件进行:反应温度为30℃、振荡速度为150rpm、反应时间为24小时、反应体积为50毫升、反应的pH值分别为7.4。In this embodiment, the ammonium thiosulfate solution is divided into three groups A, B, and C according to the concentration of the ammonium thiosulfate solution used, and each group undergoes two desorption reactions. First, each group adds 0.2M ammonium thiosulfate solution to 2.0 mg of thiourea graphene with gold ions adsorbed (the content of gold ions adsorbed per gram of thiourea graphene is 2500 mg) to perform the first Second desorption reaction. Then, after the first desorption reaction is completed, the three groups A, B, and C are respectively used for the second desorption reaction with 0.05, 0.1 or 0.2M ammonium thiosulfate solution. In addition, the first desorption reaction and the second desorption reaction are carried out according to the following reaction conditions: the reaction temperature is 30°C, the shaking speed is 150 rpm, the reaction time is 24 hours, the reaction volume is 50 ml, and the pH value of the reaction Respectively 7.4.
由图3D的结果可知,第一次脱附反应就可以使大部分的金离子从硫脲石墨烯上脱附,且具有约93%以上的脱附效率。而在第二次脱附反应中,以0.2M的硫代硫酸铵溶液(C组)可再增加约1.4%的脱附效率。也就是说,以硫代硫酸铵溶液进行脱附反应,可以使硫脲石墨烯上的金离子脱附的脱附效率为93%至96%。From the results in Figure 3D, it can be seen that the first desorption reaction can desorb most of the gold ions from the thiourea graphene, and the desorption efficiency is about 93% or more. In the second desorption reaction, 0.2M ammonium thiosulfate solution (group C) can increase the desorption efficiency by about 1.4%. That is to say, the desorption reaction with ammonium thiosulfate solution can make the desorption efficiency of gold ions on the thiourea graphene be 93% to 96%.
须要说明的是,在本实施例中,脱附效率是依据公式2来计算。公式2:脱附效率(%)=Mt/M0×100%,其中M0为脱附反应前的硫脲石墨烯上的金离子的重量(毫克),Mt为脱附反应后的金离子于溶液中的重量(毫克)。It should be noted that in this embodiment, the desorption efficiency is calculated according to Formula 2. Formula 2: Desorption efficiency (%)=Mt/M0×100%, where M0 is the weight (mg) of gold ions on the thiourea graphene before the desorption reaction, and Mt is the gold ions in the solution after the desorption reaction The weight in milligrams.
值得说明的是,为了进一步得知硫脲石墨烯对金离子的吸附效果,可将上述实施例的实验数据套用至Langmuir吸附方程式中,以进行等温吸附曲线的模拟,其结果如图4所示。由图4的模拟结果可知,等温吸附曲线的相关系数(correlation coefficient)R2为0.91,且每克硫 脲石墨烯对金离子的饱和吸附容量为833.33毫克。It is worth noting that in order to further understand the adsorption effect of thiourea graphene on gold ions, the experimental data of the above examples can be applied to the Langmuir adsorption equation to simulate the adsorption isotherm curve. The results are shown in Figure 4. . From the simulation results in Figure 4, it can be seen that the correlation coefficient R2 of the adsorption isotherm curve is 0.91, and the saturated adsorption capacity of gold ions per gram of thiourea graphene is 833.33 mg.
由于上述吸附实验皆以金离子的浓度为10毫克/升为例,但真实环境的废水中,其金离子的浓度可能比10毫克/升还低,且可能同时含有其他的金属离子,例如铜离子、铅离子、锌离子或其组合。因此,以下将以不同的实施例来探讨硫脲石墨烯对金离子的最低可吸附浓度,并探讨硫脲石墨烯对金离子和其他金属离子的选择性。Since the above adsorption experiments all take the gold ion concentration of 10 mg/L as an example, the concentration of gold ions in the wastewater in the real environment may be lower than 10 mg/L, and may also contain other metal ions, such as copper. Ions, lead ions, zinc ions, or combinations thereof. Therefore, in the following, different examples will be used to discuss the minimum adsorbable concentration of thiourea graphene for gold ions, and to discuss the selectivity of thiourea graphene for gold ions and other metal ions.
实施例6:比较氧化石墨烯与硫脲石墨烯,其分别对金离子、铜离子、铅离子及锌离子的吸附效率Example 6: Comparison of graphene oxide and graphene thiourea, respectively, the adsorption efficiency of gold ions, copper ions, lead ions and zinc ions
在本实施例中,以2.0毫克的氧化石墨烯(或2.0毫克的硫脲石墨烯)分别与浓度为10毫克/升的金离子(标示为Au)、浓度为20毫克/升的铜离子(标示为Cu)、浓度为20毫克/升的铅离子(标示为Pb)、浓度为20毫克/升的锌离子(标示为Zn)进行吸附反应,且其反应条件为:反应温度为30℃、振荡速度为150rpm、pH值为2、反应体积为50毫升、反应时间为96小时。In this embodiment, 2.0 mg of graphene oxide (or 2.0 mg of thiourea graphene) is used with gold ions (labeled as Au) at a concentration of 10 mg/L and copper ions at a concentration of 20 mg/L ( The adsorption reaction is carried out with lead ions with a concentration of 20 mg/L (labeled as Pb), and zinc ions with a concentration of 20 mg/L (labeled as Zn), and the reaction conditions are: reaction temperature of 30°C, The shaking speed is 150 rpm, the pH value is 2, the reaction volume is 50 ml, and the reaction time is 96 hours.
由图5A的结果可知,氧化石墨烯对金离子的吸附效率约为12%,硫脲石墨烯对金离子的吸附效率约为98%,且硫脲石墨烯对铜离子、铅离子及锌离子皆不具有吸附效率。因此,相较于氧化石墨烯,硫脲石墨烯对金离子具有较高的吸附效率。此外,相较于铜离子、铅离子及锌离子,硫脲石墨烯对金离子具有高选择性。From the result of Figure 5A, it can be seen that the adsorption efficiency of graphene oxide on gold ions is about 12%, the adsorption efficiency of thiourea graphene on gold ions is about 98%, and the adsorption efficiency of thiourea graphene on copper ions, lead ions, and zinc ions None of them have adsorption efficiency. Therefore, compared with graphene oxide, graphene thiourea has a higher adsorption efficiency for gold ions. In addition, graphene thiourea has high selectivity to gold ions compared to copper ions, lead ions, and zinc ions.
实施例7:硫脲石墨烯对废水中的金离子、铜离子、铅离子及锌离子的选择性Example 7: Selectivity of thiourea graphene to gold ions, copper ions, lead ions and zinc ions in wastewater
在本实施例中,依据废水的组成成份及其含量分为实验例1、实验例2以及实验例3。其中,实验例1的废水包括浓度为10毫克/升的金离子、浓度为20毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例2的废水包括浓度为1毫克/升的金离子、浓度为20毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例3的废水包括浓度为0.1毫克/升的金离子、浓度为20毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例4的废水包括浓度为0.01毫克/升的金离子、浓度为20毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。而实验例1、实验例2、实验例3以及实验例4的反应条件皆为:硫脲石墨烯为2.0毫克、反应温度为30℃、振荡速度为150rpm、pH值为2、反应体积为50毫升、反应时间为96小时。In this embodiment, the wastewater is divided into experimental example 1, experimental example 2, and experimental example 3 according to the composition and content of the wastewater. Among them, the wastewater of Experimental Example 1 includes gold ions with a concentration of 10 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 2 includes gold ions with a concentration of 1 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 3 includes gold ions with a concentration of 0.1 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 4 includes gold ions with a concentration of 0.01 mg/L, copper ions with a concentration of 20 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The reaction conditions of Experimental Example 1, Experimental Example 2, Experimental Example 3, and Experimental Example 4 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50. The reaction time is 96 hours.
由图5B的结果可知,在实验例1中,硫脲石墨烯对金离子的吸附效率为98.3±0.8%,但对铜离子、铅离子及锌离子皆不具有吸附效率。在实验例3中,硫脲石墨烯对金离子的吸附效率为98.9±0.3%,对铅离子的吸附效率约为1%至2%,但对铜离子及锌离子皆不具有吸附效率。在实验例4中,硫脲石墨烯对金离子的吸附效率为100%,但对铜离子、铅离子及锌离子皆不具有吸附效率。因此,硫脲石墨烯对金离子的最低可吸附浓度(最低吸附极限)为0.01毫克/升。此外,当金离子为0.01毫克/升至10毫克/升时,硫脲石墨烯对金离子皆具有高选择性以及98%以上的吸附效率。It can be seen from the result of FIG. 5B that in Experimental Example 1, the adsorption efficiency of thiourea graphene for gold ions is 98.3±0.8%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions. In Experimental Example 3, the adsorption efficiency of thiourea graphene for gold ions is 98.9±0.3%, and the adsorption efficiency for lead ions is about 1% to 2%, but it has no adsorption efficiency for copper ions and zinc ions. In Experimental Example 4, the adsorption efficiency of thiourea graphene for gold ions is 100%, but it has no adsorption efficiency for copper ions, lead ions, and zinc ions. Therefore, the lowest adsorbable concentration (lowest adsorption limit) of thiourea graphene for gold ions is 0.01 mg/L. In addition, when the gold ion is 0.01 mg/L to 10 mg/L, the thiourea graphene has high selectivity for gold ions and an adsorption efficiency of more than 98%.
实施例8:废水中的铜离子浓度对硫脲石墨烯的吸附效率的影响Example 8: The effect of copper ion concentration in wastewater on the adsorption efficiency of thiourea graphene
在本实施例中,依据废水的组成成份及其含量分为实验例5、实验例6、实验例7以及实验例8。其中,实验例5的废水包括浓度为10毫克/升的金离子、浓度为100毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例6的废水包括浓度为1毫克/升的金离子、浓度为100毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例7的废水包括浓度为0.1毫克/升的金离子、浓度为100毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。实验例8的废水包括浓度为 0.01毫克/升的金离子、浓度为100毫克/升的铜离子、浓度为20毫克/升的铅离子、浓度为20毫克/升的锌离子。而实验例5、实验例6、实验例7以及实验例8的反应条件皆为:硫脲石墨烯为2.0毫克、反应温度为30℃、振荡速度为150rpm、pH值为2、反应体积为50毫升、反应时间为96小时。In this embodiment, the wastewater is divided into experimental example 5, experimental example 6, experimental example 7, and experimental example 8 according to the composition and content of the wastewater. The wastewater of Experimental Example 5 includes gold ions with a concentration of 10 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 6 includes gold ions with a concentration of 1 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 7 includes gold ions with a concentration of 0.1 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The wastewater of Experimental Example 8 includes gold ions with a concentration of 0.01 mg/L, copper ions with a concentration of 100 mg/L, lead ions with a concentration of 20 mg/L, and zinc ions with a concentration of 20 mg/L. The reaction conditions of experimental example 5, experimental example 6, experimental example 7 and experimental example 8 are: thiourea graphene is 2.0 mg, the reaction temperature is 30°C, the oscillation speed is 150 rpm, the pH value is 2, and the reaction volume is 50. The reaction time is 96 hours.
由图5C的结果可知,相较于图5B的实验例1,实验例5中的硫脲石墨烯对金离子的吸附效率约略降低为95.4±0.5%,但对铜离子、铅离子及锌离子仍不具有吸附效率。此外,相较于图5B的实验例3,实验例7中的硫脲石墨烯对金离子的吸附效率为98±1.5%,对铅离子的吸附效率仍约为1%至2%,但对铜离子及锌离子仍不具有吸附效率。相较于图5B的实验例4,实验例8中的硫脲石墨烯对金离子的吸附效率为100%,对铅离子的吸附效率约为5%,但对铜离子及锌离子仍不具有吸附效率。因此,纵使提高废水中的铜离子的浓度,硫脲石墨烯对金离子仍具有高选择性以及95%至100%的吸附效率。It can be seen from the results of Figure 5C that compared with Experimental Example 1 in Figure 5B, the adsorption efficiency of thiourea graphene for gold ions in Experimental Example 5 is slightly reduced to 95.4±0.5%, but for copper ions, lead ions, and zinc ions. It still does not have adsorption efficiency. In addition, compared to Experimental Example 3 in Figure 5B, the thiourea graphene in Experimental Example 7 has an adsorption efficiency of 98±1.5% for gold ions, and the adsorption efficiency for lead ions is still about 1% to 2%, but the Copper ions and zinc ions still have no adsorption efficiency. Compared with Experimental Example 4 in Figure 5B, the thiourea graphene in Experimental Example 8 has an adsorption efficiency of 100% for gold ions and an adsorption efficiency of about 5% for lead ions, but it still has no effect on copper ions and zinc ions. Adsorption efficiency. Therefore, even if the concentration of copper ions in the wastewater is increased, graphene thiourea still has high selectivity for gold ions and an adsorption efficiency of 95% to 100%.
实施例9:硫脲石墨烯沸石的制备以及定性Example 9: Preparation and characterization of thiourea graphene zeolite
在本实施例中,例如是以以下步骤来制备硫脲石墨烯沸石,但不以此为限。首先,将沸石浸在含3-氨基丙基三乙氧基硅烷及乙醇混和溶液中反应4小时后,将沸石于50℃下干燥24小时,以获得表面有机修饰沸石。随后,将氧化石墨烯与超纯水混合以形成氧化石墨烯的胶体悬浮液,将硫脲溶解在超纯水中,以形成硫脲溶液。最后,将硫脲溶液加入于氧化石墨烯的胶体悬浮液中,以形成硫脲石墨烯混和溶液后再放入有机修饰沸石,在80℃下反应4小时,最后将固体于50℃下干燥24小时,获得硫脲石墨烯沸石。In this embodiment, for example, the following steps are used to prepare the thiourea graphene zeolite, but it is not limited thereto. First, after immersing the zeolite in a mixed solution containing 3-aminopropyltriethoxysilane and ethanol for 4 hours, the zeolite is dried at 50° C. for 24 hours to obtain a surface organically modified zeolite. Subsequently, graphene oxide is mixed with ultrapure water to form a colloidal suspension of graphene oxide, and thiourea is dissolved in ultrapure water to form a thiourea solution. Finally, the thiourea solution was added to the colloidal suspension of graphene oxide to form a thiourea-graphene mixed solution, and then put into the organically modified zeolite, reacted at 80°C for 4 hours, and finally the solid was dried at 50°C for 24 hours After hours, thiourea graphene zeolite was obtained.
硫脲石墨烯沸石外观呈现黑色,并由包括沸石、石墨烯及硫脲等多个单元件所构成,其中,石墨烯是一种由碳原子以sp2杂化轨道组成六角型成蜂巢晶格的平面薄膜,只有一个碳原子厚度的二维材料,在经硫脲改质后,外观呈现高度折叠的三维棱线结构,由径向尺寸为2–6μm的石墨烯片构成,石墨烯片彼此交叉连接形成具有50nm以上的大孔结构。硫脲石墨烯沸石的结构是以沸石为基体,沸石外表层由包含石墨烯及硫脲组成的硫脲石墨烯所包覆,硫脲石墨烯的化学结构式如式(I)所示。The appearance of thiourea graphene zeolite is black, and it is composed of multiple unit elements including zeolite, graphene and thiourea. Among them, graphene is a kind of hexagonal honeycomb lattice composed of carbon atoms and sp2 hybrid orbitals. A flat film, a two-dimensional material with the thickness of only one carbon atom. After being modified by thiourea, the appearance presents a highly folded three-dimensional ridgeline structure. It is composed of graphene sheets with a radial size of 2-6μm, and the graphene sheets cross each other. The connection forms a macroporous structure with a size of 50 nm or more. The structure of thiourea graphene zeolite is based on zeolite, and the outer surface of the zeolite is covered by thiourea graphene composed of graphene and thiourea. The chemical structure of thiourea graphene is shown in formula (I).
Figure PCTCN2020116296-appb-000007
Figure PCTCN2020116296-appb-000007
接着,对硫脲石墨烯沸石表面的元素成份及其含量进行分析,其结果如表2所示。Next, the element composition and content on the surface of the thiourea graphene zeolite were analyzed, and the results are shown in Table 2.
表2Table 2
 To C(%)C(%) O(%)O(%) H(%)H(%) N(%)N(%) S(%)S(%)
硫脲石墨烯沸石Thiourea Graphene Zeolite 50.7850.78 27.3027.30 3.653.65 3.073.07 4.964.96
由表2元素分析的结果可知材料表面碳、氮及硫含量分别为50.78%、3.07%及4.96%,显示硫脲石墨烯已负载于沸石基材上面。From the results of elemental analysis in Table 2, it can be seen that the carbon, nitrogen, and sulfur content on the surface of the material are 50.78%, 3.07%, and 4.96%, respectively, indicating that graphene thiourea has been supported on the zeolite substrate.
接着,由图6A的X光衍射的分析结果可知,硫脲石墨烯沸石于2θ=12.46o及23.68o具有明显的衍射峰。Next, from the X-ray diffraction analysis result of FIG. 6A, it can be seen that the thiourea graphene zeolite has obvious diffraction peaks at 2θ=12.46° and 23.68°.
由图6B的扫描式电子显微镜的分析结果可知,在2000倍的放大图中,硫脲石墨烯沸石的表面具有高度折叠的三维棱线结构。From the analysis result of the scanning electron microscope in FIG. 6B, it can be seen that in the 2000 times magnification, the surface of the thiourea graphene zeolite has a highly folded three-dimensional ridgeline structure.
实施例10:反应的pH值对硫脲石墨烯沸石吸附效率的影响Example 10: The influence of the pH value of the reaction on the adsorption efficiency of thiourea graphene zeolite
在本实施例中,试验条件为:硫脲石墨烯沸石为0.01克、金离子浓度为10毫升/公升、反应温度为30℃、振荡速度为150rpm、反应时间为24小时、反应体积为50毫升,且反应的pH值分别为0、1、2、3、4、5、6、7、8、9及10。In this embodiment, the test conditions are: 0.01 g of thiourea graphene zeolite, a gold ion concentration of 10 ml/liter, a reaction temperature of 30°C, an oscillation speed of 150 rpm, a reaction time of 24 hours, and a reaction volume of 50 ml , And the pH of the reaction is 0, 1, 2, 3, 4, 5, 6, 7, 8, 9 and 10, respectively.
由图7结果可知当反应的pH值为0~3时,硫脲石墨烯沸石对金离子的吸附效率可达90%以上,当反应的pH值为4~5时,硫脲石墨烯沸石对金离子的吸附效率约为60%~70%。当反应的pH值在6~10时,硫脲石墨烯沸石对金离子的吸附效率则快速降低至10%以下。It can be seen from the results in Figure 7 that when the pH of the reaction is 0 to 3, the adsorption efficiency of thiourea graphene zeolite for gold ions can reach more than 90%. When the pH of the reaction is 4 to 5, the thiourea graphene zeolite The adsorption efficiency of gold ions is about 60% to 70%. When the pH value of the reaction is 6-10, the adsorption efficiency of the thiourea graphene zeolite for gold ions is rapidly reduced to below 10%.
实施例11:硫脲石墨烯沸石对金离子的饱和吸附容量测定Example 11: Determination of the saturated adsorption capacity of thiourea graphene zeolite for gold ions
在本实施例中,为了进一步得知硫脲石墨烯沸石对金离子的吸附效果,使用硫脲石墨烯沸石于不同金离子浓度的溶液中进行吸附试验,将所获得的实验数据套用至Langmuir吸附方程式中,以进行等温吸附曲线的模拟,其结果如图8所示。由图8的模拟结果可知,等温吸附曲线的相关系数(correlation coefficient)R2为0.97,且每克硫脲石墨烯沸石对金离子的饱和吸附容量为97.1毫克。In this example, in order to further understand the adsorption effect of thiourea graphene zeolite on gold ions, thiourea graphene zeolite was used to perform adsorption experiments in solutions of different gold ion concentrations, and the obtained experimental data was applied to Langmuir adsorption In the equation, a simulation of the adsorption isotherm curve is performed, and the result is shown in Figure 8. It can be seen from the simulation results in Fig. 8 that the correlation coefficient R2 of the adsorption isotherm curve is 0.97, and the saturated adsorption capacity of gold ions per gram of thiourea graphene zeolite is 97.1 mg.
实施例12:硫脲石墨烯沸石分别对废水中的金离子、铜离子、铅离子及锌离子的选择性Example 12: Selectivity of thiourea graphene zeolite to gold ions, copper ions, lead ions and zinc ions in wastewater
在本实施例中,依据废水的组成成分及其含量分别为实验例1的废水包括浓度为1毫升/公升的金离子、浓度为100毫升/公升的铜离子、浓度为20毫升/公升的铅离子、浓度为20毫升/公升的锌离子、浓度为20毫升/公升的镍离子。实施例2的废水包括浓度为10毫升/公升的金离子、浓度为100毫升/公升的铜离子、浓度为20毫升/公升的铅离子、浓度为20毫升/公升的锌离子、浓度为20毫升/公升的镍离子。In this embodiment, according to the composition and content of the wastewater, the wastewater of Experimental Example 1 includes gold ions with a concentration of 1 ml/liter, copper ions with a concentration of 100 ml/liter, and lead with a concentration of 20 ml/liter. Ions, zinc ions with a concentration of 20 ml/liter, nickel ions with a concentration of 20 ml/liter. The wastewater of Example 2 includes gold ions with a concentration of 10 ml/liter, copper ions with a concentration of 100 ml/liter, lead ions with a concentration of 20 ml/liter, zinc ions with a concentration of 20 ml/liter, and a concentration of 20 ml. /L of nickel ion.
而实验例1及实验例2的反应条件皆为:硫脲石墨烯沸石为0.01克、反应温度为30℃、振荡速度为150rpm、反应时间为24小时、反应体积为50毫升。The reaction conditions of Experimental Example 1 and Experimental Example 2 are: 0.01 g of thiourea graphene zeolite, reaction temperature of 30° C., oscillation speed of 150 rpm, reaction time of 24 hours, and reaction volume of 50 ml.
由图9的结果可知,在实验例1中硫脲石墨烯沸石对金离子的吸附效率约为93.13%,对铜离子、铅离子、锌离子及镍离子吸附效率皆低于5%。在实验例2中,硫脲石墨烯沸石对金离子吸附效率为94.05%,对铜离子、铅离子、锌离子、镍离子的吸附效率分别为0.86%、2.73%、4.36%、0.81%。因此,硫脲石墨烯沸石对金离子具有高选择性以及93%~94%的吸附效率。It can be seen from the results of FIG. 9 that in Experimental Example 1, the adsorption efficiency of thiourea graphene zeolite for gold ions is about 93.13%, and the adsorption efficiency for copper ions, lead ions, zinc ions, and nickel ions are all less than 5%. In Experimental Example 2, the adsorption efficiency of thiourea graphene zeolite for gold ions was 94.05%, and the adsorption efficiency for copper ions, lead ions, zinc ions, and nickel ions were 0.86%, 2.73%, 4.36%, and 0.81%, respectively. Therefore, thiourea graphene zeolite has high selectivity for gold ions and an adsorption efficiency of 93% to 94%.
综上所述,在本发明提供的使用硫脲石墨烯沸石及其用于吸附金的用途中,通过硫脲石墨烯沸石对于金离子的高选择性,使得在利用硫脲石墨烯沸石对一含金溶液中的金离子进行吸附反应时,可具有较低的吸附极限、较佳的吸附效率以及较高的饱和吸附容量。In summary, in the use of thiourea graphene zeolite and its use for gold adsorption provided by the present invention, the high selectivity of thiourea graphene zeolite for gold ions makes the use of thiourea graphene zeolite to When the gold ion in the gold-containing solution undergoes an adsorption reaction, it can have a lower adsorption limit, a better adsorption efficiency, and a higher saturated adsorption capacity.
虽然本发明已以实施例揭示如上,然其并非用以限定本发明,任何所属技术领域中技术人员,在不脱离本发明的精神和范围内,当可作些许的更改与润饰,故本发明的保护范围当视权利要求所界定的为准。Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention. Anyone skilled in the art, without departing from the spirit and scope of the present invention, can make some changes and modifications, so the present invention The scope of protection shall be subject to what is defined in the claims.

Claims (24)

  1. 一种石墨烯组合物,其特征在于,所述石墨烯组合物至少包含一式(I)结构的化合物:A graphene composition, characterized in that the graphene composition at least comprises a compound of formula (I):
    Figure PCTCN2020116296-appb-100001
    Figure PCTCN2020116296-appb-100001
  2. 根据权利要求1所述的石墨烯组合物,其特征在于,所述石墨烯组合物的氮含量为2~4重量%,且硫含量为20~23重量%。The graphene composition of claim 1, wherein the nitrogen content of the graphene composition is 2 to 4% by weight, and the sulfur content is 20 to 23% by weight.
  3. 一种使用一石墨烯组合物于一含金溶液中吸附一金离子的方法,其特征在于,所述石墨烯组合物至少包含一式(I)结构的化合物:A method for using a graphene composition to adsorb a gold ion in a gold-containing solution, wherein the graphene composition at least comprises a compound of formula (I):
    Figure PCTCN2020116296-appb-100002
    Figure PCTCN2020116296-appb-100002
  4. 根据权利要求3所述的方法,其特征在于,所述含金溶液的pH值为2至10。The method according to claim 3, wherein the pH of the gold-containing solution is 2-10.
  5. 根据权利要求3所述的方法,其特征在于,所述石墨烯组合物对所述金离子的吸附效率为45%至100%。The method according to claim 3, wherein the adsorption efficiency of the graphene composition to the gold ions is 45% to 100%.
  6. 根据权利要求3所述的方法,其特征在于,每克所述石墨烯组合物对所述金离子的饱和吸附容量为810至850毫克。The method according to claim 3, wherein the saturated adsorption capacity of the gold ions per gram of the graphene composition is 810 to 850 mg.
  7. 根据权利要求3所述的方法,其特征在于,当所述含金溶液还包括一铜离子、一铅离子、一锌离子或其组合时,所述石墨烯组合物对所述铅离子的吸附效率为1%至2%,且对所述铜离子及所述锌离子的吸附效率为0%。The method of claim 3, wherein when the gold-containing solution further includes a copper ion, a lead ion, a zinc ion, or a combination thereof, the graphene composition adsorbs the lead ion The efficiency is 1% to 2%, and the adsorption efficiency of the copper ion and the zinc ion is 0%.
  8. 一种于一含金溶液中处理一金离子的方法,其特征在于,包含一步骤:A method for processing a gold ion in a gold-containing solution, which is characterized in that it comprises a step:
    将一包含式(I)结构化合物的石墨烯组合物与所述含金溶液中之所述金离子接触:Contacting a graphene composition containing a structure compound of formula (I) with the gold ions in the gold-containing solution:
    Figure PCTCN2020116296-appb-100003
    Figure PCTCN2020116296-appb-100003
  9. 根据权利要求8所述的方法,其特征在于,所述的方法还包含一步骤:以一脱附剂使所述金离子从所述包含式(I)化合物的石墨烯组合物上脱附。8. The method according to claim 8, wherein the method further comprises a step of desorbing the gold ions from the graphene composition containing the compound of formula (I) with a desorbent.
  10. 根据权利要求9所述的方法,其特征在于,所述金离子的脱附效率为90%至96%。The method according to claim 9, wherein the desorption efficiency of the gold ions is 90% to 96%.
  11. 一种石墨烯复合物,其特征在于,所述石墨烯复合物包含:A graphene composite, characterized in that the graphene composite comprises:
    一载体,以及A carrier, and
    一包含式(I)结构化合物的石墨烯组合物,所述石墨烯组合物位于所述载体的表面:A graphene composition comprising a structure compound of formula (I), the graphene composition being located on the surface of the carrier:
    Figure PCTCN2020116296-appb-100004
    Figure PCTCN2020116296-appb-100004
  12. 根据权利要求11所述的石墨烯复合物,其特征在于,所述载体为一沸石。The graphene composite of claim 11, wherein the carrier is a zeolite.
  13. 根据权利要求12所述的石墨烯复合物,其特征在于,所述石墨烯复合物经X光衍射于2θ=12.46°及23.68°具有明显的衍射峰。The graphene composite of claim 12, wherein the graphene composite has obvious diffraction peaks at 2θ=12.46° and 23.68° by X-ray diffraction.
  14. 根据权利要求12所述的石墨烯复合物,其特征在于,所述石墨烯复合物表面的碳含量为49~52重量%。The graphene composite according to claim 12, wherein the carbon content on the surface of the graphene composite is 49-52% by weight.
  15. 根据权利要求12所述的石墨烯复合物,其特征在于,所述石墨烯复合物表面的氮含量为2~5重量%。The graphene composite according to claim 12, wherein the nitrogen content on the surface of the graphene composite is 2 to 5% by weight.
  16. 根据权利要求12所述的石墨烯复合物,其特征在于,所述石墨烯复合物表面的硫含量为3~6重量%。The graphene composite according to claim 12, wherein the sulfur content on the surface of the graphene composite is 3 to 6% by weight.
  17. 一种制造硫脲石墨烯沸石的方法,其特征在于,包括以下步骤:A method for manufacturing thiourea graphene zeolite is characterized in that it comprises the following steps:
    a)将一沸石与一含3-氨基丙基三乙氧基硅烷及乙醇混和溶液反应,得到一反应后沸石;a) Reacting a zeolite with a mixed solution containing 3-aminopropyltriethoxysilane and ethanol to obtain a reacted zeolite;
    b)将氧化石墨烯与水混合以形成一悬浮液;b) Mixing graphene oxide with water to form a suspension;
    c)将硫脲溶解在水中以形成一硫脲溶液;以及c) dissolving thiourea in water to form a thiourea solution; and
    d)将所述硫脲溶液、所述悬浮液与所述反应后沸石相混和并加热,以形成一硫脲石墨烯沸石。d) The thiourea solution, the suspension and the reacted zeolite are mixed and heated to form a thiourea graphene zeolite.
  18. 根据权利要求17所述的方法,其特征在于,加热范围为75℃至85℃。The method according to claim 17, wherein the heating range is 75°C to 85°C.
  19. 一种使用一石墨烯复合物于一含金溶液中吸附金离子的方法,其特征在于,所述石墨烯复合物包含:A method for using a graphene composite to adsorb gold ions in a gold-containing solution, wherein the graphene composite comprises:
    一载体,以及A carrier, and
    一包含式(I)结构化合物的石墨烯组合物,所述石墨烯组合物位于所述载体的表面:A graphene composition comprising a structure compound of formula (I), the graphene composition being located on the surface of the carrier:
    Figure PCTCN2020116296-appb-100005
    Figure PCTCN2020116296-appb-100005
  20. 根据权利要求19所述的方法,其特征在于,所述石墨烯复合物的所述载体为一沸石。The method of claim 19, wherein the carrier of the graphene composite is a zeolite.
  21. 根据权利要求19所述的方法,其特征在于,所述含金溶液的pH值为0至10。The method of claim 19, wherein the pH of the gold-containing solution is 0-10.
  22. 根据权利要求20所述的方法,其特征在于,所述石墨烯复合物对所述金离子的吸附效率为60%至100%。22. The method of claim 20, wherein the adsorption efficiency of the graphene composite for the gold ions is 60% to 100%.
  23. 根据权利要求20所述的方法,其特征在于,每克所述石墨烯复合物对所述金离子的饱和吸附容量为90至100毫克。22. The method of claim 20, wherein the saturated adsorption capacity of the gold ions per gram of the graphene composite is 90 to 100 mg.
  24. 根据权利要求20所述的方法,其特征在于,当所述含金溶液还包括铜离子、铅离子、锌离子、镍离子或其组合时,所述石墨烯复合物对所述铜离子的吸附效率为0.5%至5%,对所述铅离子的吸附效率为2%至5%,对锌离子的吸附效率为0%至5%,以及对镍离子的吸附效率为0.5%至5%。The method according to claim 20, wherein when the gold-containing solution further includes copper ions, lead ions, zinc ions, nickel ions, or a combination thereof, the graphene composite adsorbs the copper ions The efficiency is 0.5% to 5%, the adsorption efficiency for the lead ions is 2% to 5%, the adsorption efficiency for zinc ions is 0% to 5%, and the adsorption efficiency for nickel ions is 0.5% to 5%.
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