CN113893821B - Porous carbon material noble metal adsorbent based on nitrogen and sulfur doping and preparation method thereof - Google Patents

Porous carbon material noble metal adsorbent based on nitrogen and sulfur doping and preparation method thereof Download PDF

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CN113893821B
CN113893821B CN202111200874.8A CN202111200874A CN113893821B CN 113893821 B CN113893821 B CN 113893821B CN 202111200874 A CN202111200874 A CN 202111200874A CN 113893821 B CN113893821 B CN 113893821B
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carbon material
nitrogen
porous carbon
sulfur doping
sulfur
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CN113893821A (en
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刘苏涛
潘有春
陈志�
梁燕
王光应
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Anhui Yuanchen Environmental Protection Science and Technology Co Ltd
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    • 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
    • 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
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0259Compounds of N, P, As, Sb, Bi
    • 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
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0262Compounds of O, S, Se, Te
    • B01J20/0266Compounds of S

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  • Inorganic Chemistry (AREA)
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Abstract

A porous carbon material noble metal adsorbent based on nitrogen and sulfur doping relates to the technical field of noble metal adsorption recovery, and is based on the problem of low adsorption capacity of the existing gold thiosulfate ions. The carbon material has a micro porous structure, and nitrogen and sulfur elements are doped on the surface of the carbon material; the raw materials of the carbon material comprise a carbon source, a template agent and an activating agent; the carbon source is 2-aminothiazole. The invention also discloses a preparation method of the porous carbon material noble metal adsorbent based on nitrogen and sulfur doping. According to the invention, 2-aminothiazole is used as a raw material, under the action of a template agent and an activating agent, the nitrogen-sulfur doped porous carbon material is obtained through high-temperature calcination, the adsorption capacity of the carbon material can be improved through a porous structure constructed by a template method, and the adsorption capacity of gold ions can be improved through doping nitrogen and sulfur elements.

Description

Porous carbon material noble metal adsorbent based on nitrogen and sulfur doping and preparation method thereof
Technical Field
The invention relates to the technical field of noble metal adsorption recovery, in particular to a porous carbon material noble metal adsorbent based on nitrogen and sulfur doping and a preparation method thereof.
Background
Gold, silver, platinum, palladium, ruthenium, rhodium, osmium and iridium are used as 8 noble metal elements, and are widely applied to the modern technological and industrial fields of aerospace, military industry, electronic and electric appliances, traffic, petrochemical industry and the like, and have important strategic significance. Precious metal resources are rare and expensive, the recycling value of waste materials is much higher than that of common metals, and the waste materials are valuable secondary resources, so that the method for recycling the precious metals from the waste materials has important significance.
Conventional methods for recovering noble metals include ion exchange, reverse osmosis, neutral precipitation, and adsorption. The adsorption method has the advantages of low cost, easy operation, small pollution and the like, and becomes an ideal green extraction technology. The adsorption method is used for extracting noble metals, and the types of adsorbents required by the adsorption method are more, and comprise chelate resin, mesoporous materials, activated carbon and the like. The carbon material has the characteristics of acid resistance, alkali resistance, corrosion resistance, difficult poisoning, regeneration recovery and the like, and is widely concerned, but the carbon material has lower adsorption capacity to gold thiosulfate ions, so that the popularization of the gold ion adsorption technology of the carbon material is limited.
In order to improve the adsorption capacity of the carbon material to gold thiosulfate ions, 2-mercaptobenzothiazole is adopted as a doping agent in the patent CN107215872A, and the carbon material is doped by using an organic solvent or strong alkali as a solvent, but expensive doping agents are used in the process, and toxic wastes are easily generated; the patent CN109574008A uses ammonium thiocyanate to dope the carbon material, but the process requires severe conditions such as high temperature and high pressure. The porous structure is designed to improve the specific surface area and pore channels of the material and also can improve the loading capacity of the adsorbent, and the porous sodium alginate adsorbent is prepared by a template method in the patent CN109433164A, so that the adsorption capacity is improved.
Disclosure of Invention
The invention aims to solve the technical problems that the existing gold thiosulfate ion adsorption capacity is low, and the popularization of the gold ion adsorption technology of carbon materials is limited.
The invention solves the technical problems by the following technical means:
a porous carbon material noble metal adsorbent based on nitrogen and sulfur doping, wherein the carbon material has a micro porous structure, and the surface of the carbon material is doped with nitrogen and sulfur elements;
the raw materials of the carbon material comprise a carbon source, a template agent and an activating agent;
the carbon source is 2-aminothiazole;
the mass of the template agent is 2-10 times of that of the carbon source;
the mass of the activator is 5-30 times of that of the carbon source.
According to the invention, nitrogen and sulfur elements are doped on the surface of the carbon material, and the carbon material has a porous structure, so that the adsorption capacity of gold ions can be improved.
Preferably, the template agent comprises calcium hydroxide, F 127 One or both of which are mixed.
Preferably, the activator comprises H 3 PO 4 、ZnCl 2 At least one of KOH.
The invention also discloses a preparation method of the porous carbon material noble metal adsorbent based on nitrogen-sulfur doping, which comprises the following steps:
(1) Weighing 2-aminothiazole, a template agent and an activating agent with certain mass, and performing ball milling and mixing uniformly to obtain mixed powder;
(2) Placing the mixed powder obtained in the step (1) in a quartz boat, and adding N 2 Heating to 600-900 deg.c in a tubular furnace under protection for 6-20 hr to obtain black powder;
(3) Washing the black powder obtained in the step (2) with hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for multiple times;
(4) Drying the powder washed in the step (3) in a vacuum drying oven, and finally, placing the dried powder in a tube furnace in N 2 And (5) keeping the temperature of 200 ℃ for 2 hours under the atmosphere to obtain the product.
Further, the rotational speed of the ball milling in the step (1) is 380r/min.
Further, the ball milling time in the step (1) is 2 hours.
Further, the concentration of hydrochloric acid in the step (3) is 30%.
Further, deionized water and ethanol are washed 3 times in the step (3).
Further, the drying temperature in the step (4) is 70-90 ℃.
Further, the drying time in the step (4) is 5-7h.
The invention has the following beneficial effects:
1. according to the invention, nitrogen and sulfur elements are doped on the surface of the carbon material, and the carbon material has a porous structure, so that the adsorption capacity of gold ions can be improved.
2. According to the invention, 2-aminothiazole is used as a raw material, under the action of a template agent and an activating agent, the nitrogen-sulfur doped porous carbon material is obtained through high-temperature calcination, the adsorption capacity of the carbon material can be improved through a porous structure constructed by a template method, and the adsorption capacity of gold ions can be improved through doping nitrogen and sulfur elements.
3. The nitrogen-sulfur doped porous carbon material has better adsorption capacity for silver ions.
Drawings
FIG. 1 is a process flow diagram of a method for preparing a porous carbon material noble metal adsorbent based on nitrogen-sulfur doping in accordance with an embodiment of the present invention;
fig. 2 is an SEM image of the product prepared in example 1 of the present invention.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present invention more apparent, the technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings and the embodiments of the present invention, and it is apparent that the described embodiments are some embodiments of the present invention, but not all embodiments of the present invention. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
The test materials, reagents and the like used in the examples described below are commercially available unless otherwise specified.
Those of skill in the art, without any particular mention of the techniques or conditions, may follow the techniques or conditions described in the literature in this field or follow the product specifications.
Example 1
A preparation method of a porous carbon material noble metal adsorbent (NSPC 1) based on nitrogen-sulfur doping comprises the following steps:
(1) 0.1282g of 2-aminothiazole and 0.7692g of Ca (OH) were weighed out 2 0.7692g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixture is evenly mixed to obtain mixed powder;
(2) Mixing the mixture obtained in step (1)Placing the powder in a quartz boat, at N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder;
(3) Washing the black powder obtained in the step (2) with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times;
(4) Drying the powder washed in the step (3) for 6 hours at 80 ℃ in a vacuum drying oven, and finally using N in a tube furnace 2 (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, designated NSPC1.
The product NSPC1 prepared in this example was subjected to Scanning Electron Microscope (SEM) analysis, and the analysis results are shown in fig. 2.
Example 2
A preparation method of a porous carbon material noble metal adsorbent (NSPC 2) based on nitrogen-sulfur doping comprises the following steps:
(1) 0.1282g of 2-aminothiazole and 0.7692g of Ca (OH) were weighed out 2 1.2820g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixture is evenly mixed to obtain mixed powder;
(2) Placing the mixed powder obtained in the step (1) in a quartz boat, and adding N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder;
(3) Washing the black powder obtained in the step (2) with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times;
(4) Drying the powder washed in the step (3) for 6 hours at 80 ℃ in a vacuum drying oven, and finally using N in a tube furnace 2 (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, designated NSPC2.
Example 3
A preparation method of a porous carbon material noble metal adsorbent (NSPC 3) based on nitrogen-sulfur doping comprises the following steps:
(1) 0.1282g of 2-aminothiazole and 1.2820g of Ca (OH) were weighed out 2 1.2820g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixture is evenly mixed to obtain mixed powder;
(2) The step (1) is carried outIs placed in a quartz boat, at N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder;
(3) Washing the black powder obtained in the step (2) with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times;
(4) Drying the powder washed in the step (3) for 6 hours at 80 ℃ in a vacuum drying oven, and finally using N in a tube furnace 2 (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, designated NSPC3.
Comparative example 1
0.1282g of 2-methylimidazole and 0.7692g of Ca (OH) were weighed out 2 1.2820g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixed powder is prepared; placing the mixed powder in a quartz boat, at N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder; washing the black powder with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times; drying the washed powder in a vacuum drying oven at 80deg.C for 6 hr, and finally using N in a tube furnace 2 (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, which was designated as N-PC.
Comparative example 2
0.1282g of 2-methylthiophene and 0.7692g of Ca (OH) were weighed out 2 1.2820g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixed powder is prepared; placing the mixed powder in a quartz boat, at N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder; washing the black powder with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times; drying the washed powder in a vacuum drying oven at 80deg.C for 6 hr, and finally using N in a tube furnace 2 (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, designated as S-PC.
Comparative example 3
0.1282g of coke and 1.2820g of ZnCl are weighed out 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixed powder is prepared; placing the mixed powder in a quartz boat, at N 2 (30mL/min), heating to 800 ℃ in a tube furnace under the protection of the powder, and preserving heat for 12 hours to obtain black powder; washing the black powder with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times; drying the washed powder in a vacuum drying oven at 80deg.C for 6 hr, and finally using N in a tube furnace 2 And (30 mL/min) was kept at 200℃for 2 hours under an atmosphere to obtain a product, designated as C.
Comparative example 4
0.1282g of coke and 0.7692g of Ca (OH) were weighed out 2 1.2820g of ZnCl 2 Ball milling is carried out for 2 hours at the rotating speed of 380r/min, and the mixed powder is prepared; placing the mixed powder in a quartz boat, at N 2 Heating to 800 ℃ in a tube furnace under the protection of (30 mL/min) and preserving heat for 12 hours to obtain black powder; washing the black powder with 30% hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for 3 times; drying the washed powder in a vacuum drying oven at 80deg.C for 6 hr, and finally using N in a tube furnace 2 The mixture was kept at 200℃for 2 hours under an atmosphere of (30 mL/min), and the product was obtained and designated as PC.
Adsorption performance test experiments were performed on the above-prepared examples 1 to 3 and comparative examples 1 to 4.
100mL of Au (S) having a concentration of 200ppm was prepared 2 O 3 ) 2 3- The pH value of the solution (adsorption solution) is regulated to 10, 0.5g of the adsorption materials prepared in the examples and the comparative examples are added into the adsorption solution, and the adsorption is carried out for 36 hours at the constant temperature of 30 ℃, and the results are shown in the table 1, so that the invention takes 2-aminothiazole as a raw material, and under the action of a template agent and an activator, the nitrogen-sulfur doped porous carbon material is obtained through high-temperature calcination, the adsorption capacity of the carbon material can be improved through the porous structure constructed by the template method, and the adsorption capacity of gold ions can be improved through doping nitrogen and sulfur elements.
In addition, 100mL of AgNO with a concentration of 200ppm was prepared 3 The solution is tried to absorb silver ions, and the result is shown in table 2, so that the nitrogen-sulfur doped porous carbon material has better absorbing capability to silver ions.
Table 1 shows the results of adsorption efficiency of carbon material on gold thiosulfate
Sample of NSPC1 NSPC2 NSPC3 N-PC S-PC C PC
Adsorption rate of 89.7% 95.6% 91.1% 85.5% 87.3% 45.2% 53.7%
Table 2 shows the adsorption efficiency of the carbon material to silver ions
Sample of NSPC1 NSPC2 NSPC3 N-PC S-PC C PC
Adsorption rate of 43.9% 55.6% 48.2% 35.1% 41.6% 13.7% 33.7%
The above embodiments are only for illustrating the technical solution of the present invention, and are not limiting; although the invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present invention.

Claims (8)

1. An application of a porous carbon material based on nitrogen-sulfur doping in gold thiosulfate ion adsorption is characterized in that: the carbon material has a micro porous structure, and nitrogen and sulfur elements are doped on the surface of the carbon material;
the raw materials of the carbon material comprise a carbon source, a template agent and an activating agent;
the carbon source is 2-aminothiazole;
the mass of the template agent is 2-10 times of that of the carbon source, and the template agent is calcium hydroxide;
the mass of the activator is 5-30 times of that of the carbon source, and the activator is ZnCl 2
2. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 1, characterized by comprising the steps of:
(1) Weighing 2-aminothiazole, a template agent and an activating agent with certain mass, and performing ball milling and mixing uniformly to obtain mixed powder;
(2) Placing the mixed powder obtained in the step (1) in a quartz boat, and adding N 2 Heating to 600-900 deg.c in a tubular furnace under protection for 6-20 hr to obtain black powder;
(3) Washing the black powder obtained in the step (2) with hydrochloric acid to remove residual template agent and activator, and washing with deionized water and ethanol for multiple times;
(4) Drying the powder washed in the step (3) in a vacuum drying oven, and finally, placing the dried powder in a tube furnace in N 2 And (5) keeping the temperature of 200 ℃ for 2 hours under the atmosphere to obtain the product.
3. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: the rotational speed of ball milling in the step (1) is 380r/min.
4. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: the ball milling time in the step (1) is 2 hours.
5. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: the concentration of hydrochloric acid in the step (3) is 30 percent.
6. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: and (3) washing with deionized water and ethanol for 3 times in the step (3).
7. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: the drying temperature in the step (4) is 70-90 ℃.
8. Use of a porous carbon material based on nitrogen-sulfur doping for gold thiosulfate ion adsorption according to claim 2, characterized in that: the drying time in the step (4) is 5-7h.
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