CN112357906A - Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof - Google Patents

Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof Download PDF

Info

Publication number
CN112357906A
CN112357906A CN202011259848.8A CN202011259848A CN112357906A CN 112357906 A CN112357906 A CN 112357906A CN 202011259848 A CN202011259848 A CN 202011259848A CN 112357906 A CN112357906 A CN 112357906A
Authority
CN
China
Prior art keywords
nitrogen
p4vp
doped
monomodal
ultramicropore
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202011259848.8A
Other languages
Chinese (zh)
Inventor
杨正龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tongji University
Original Assignee
Tongji University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tongji University filed Critical Tongji University
Priority to CN202011259848.8A priority Critical patent/CN112357906A/en
Publication of CN112357906A publication Critical patent/CN112357906A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/15Nano-sized carbon materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • 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
    • B01J20/20Solid 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
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28064Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
    • 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
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28066Surface area, e.g. B.E.T specific surface area being more than 1000 m2/g
    • 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
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28069Pore volume, e.g. total pore volume, mesopore volume, micropore volume
    • B01J20/28071Pore volume, e.g. total pore volume, mesopore volume, micropore volume being less than 0.5 ml/g
    • 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
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28069Pore volume, e.g. total pore volume, mesopore volume, micropore volume
    • B01J20/28073Pore volume, e.g. total pore volume, mesopore volume, micropore volume being in the range 0.5-1.0 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • B22F1/0553Complex form nanoparticles, e.g. prism, pyramid, octahedron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/07Metallic powder characterised by particles having a nanoscale microstructure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/16Making metallic powder or suspensions thereof using chemical processes
    • B22F9/30Making metallic powder or suspensions thereof using chemical processes with decomposition of metal compounds, e.g. by pyrolysis
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • C10L3/104Carbon dioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/102Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4806Sorbents characterised by the starting material used for their preparation the starting material being of inorganic character
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • C10L2290/542Adsorption of impurities during preparation or upgrading of a fuel
    • 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
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2
    • 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
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • Nanotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention relates to a method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using an in-situ amorphous cobalt template method, and a method and application thereof, wherein P4VP and CoCl are used2·6H2O as a raw material, Co2+Form Co-P with P4VP4VP in Co2+From Co-P4VP, P4VP was converted to Co-NDC by ClInducing and Co-N bond confinement effect to induce the formation of amorphous Co nanoclusters, coating the amorphous Co nanoclusters in the carbon nanosheets converted from P4VP, and removing the amorphous Co nanoclusters through acid etching to form Co-NDPC with ultramicropores with the pore diameter of 0.5 +/-0.05 nm. Compared with the prior art, the method effectively avoids the defects of corrosivity, poor safety, complex process and the like existing in the traditional activation method or template method, and the synthesized Co-NDPC is CH with a very good application prospect4/C2H2/C2H6/C3H8/CO2/N2Adsorbing the separating agent.

Description

Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof
Technical Field
The invention belongs to the technical field of gas adsorption separation materials, and particularly relates to a nitrogen-doped unimodal ultramicropore carbon nanosheet synthesized by an in-situ amorphous cobalt template method, a method and application thereof.
Background
Natural gas is composed mainly of methane (CH)470-90%) and acetylene (C)2H2) Ethane (C)2H6) Propane (C)3H8) Carbon dioxide (CO)2) And the like, and is one of the most important energy and chemical raw materials in the industrial society. E.g. CH4Having the highest specific heating value (55.7kJ/g) is considered to be one of the most promising energy candidates in the future; c2H6And C3H8Dehydrogenation and C2H2Hydrogenation is an industrial production C2H4And C3H6Of a main raw material, and C2H4And C3H6But also is a basic chemical for producing bulk commodities such as polypropylene, polyester, polyethylene and the like. Based on the specificity of each component, other components in the natural gas are mixed with CH4The separation has very important significance for realizing the high-efficiency utilization of resources. In addition, fossil fuel combustion produces CO2The emission is the main cause of greenhouse effect, which causes global warming, glacier melting and sea level rise, and is one of the biggest environmental problems facing human in this century. Although the combustion products of natural gas are cleaner than coal and oil, it still emits significant amounts of CO2. Therefore, how to capture and separate CO in flue gas2Also has important research significance. Furthermore, CO is utilized2The direct preparation of industrial products such as carbon monoxide, methanol, ethylene, ethanol and the like by electrocatalysis reduction is one of the current research hotspots2The capture and separation of the protein have great economic value and prospect.
The low-temperature rectification separation of natural gas and the absorption of flue gas alkali liquor are the classical methods for solving the problems. However, the rectification separation has complex process and large energy consumption, and the alkali liquor absorption has difficult regeneration and is not beneficial to CO2The subsequent utilization problem. The adsorption separation has simple operation process, energy saving, high efficiency and easy regenerationAnd the like are considered as the most promising alternative technologies. The adsorbent is the core of the technology and determines the separation efficiency of the whole process. Nitrogen-doped porous carbon (NDPCs) have the advantages of rich raw materials, stable physicochemical properties, strong weather resistance, low cost and the like, and are considered to be one of the most promising adsorbents. Therefore, the development of high performance NDPCs has been the focus and difficulty of adsorption separation engineering. In this regard, Zhang et al [ Wang J, Krishna R, Yang T, et al, Nitrogen-rich micropous carbons for high selectivity section of light hydrocarbons [ J].Journal of Materials Chemistry A 2016,4:13957-13966]Nitrogen-doped porous carbon NCA 700 is synthesized by KOH activation of a nitrogen-rich polymer precursor. At 298K and 1bar, NCA 700 vs. C2H2、C2H6And C3H8Adsorption capacity of (2) and corresponding x/CH4IAST selectivity reaches 6.39(47.1), 7.59(65.7) and 11.56 mmol.g-1(501.9). Liang et al [ Liang W, Zhang Y, Wang X, et al. alpha. high surface area activated porous carbonates for the effective adsorption of methane and ethylene [ J].Chemical Engineering Science 2017,162:192-202]Porous carbon A-AC-3 is synthesized by KOH activated asphalt. At 298K and 1bar, A-AC-3 is opposite to C2H6And C3H8Adsorption capacity of (2) and corresponding x/CH4IAST selectivity reached 7.09(16.9) and 11.34 mmol. multidot.g-1(88.8). Ashourirad et al [ Ashourirad B, Sekizkardes A K, Altaraweh S, et al].Chemistry of Materials 2015,27:1349-1358]Nitrogen-doped porous carbon CPC 550 was prepared by KOH activation of a benzimidazole crosslinked polymer. CO of CPC 550 at 298K and 1bar2Adsorption capacity and corresponding CO2/N2IAST selectivities of 5.8 and 59 mmol-g, respectively-1. Furthermore, Aijaz et al [ Aijaz A, Fujiwara N, Xu Q. from metal-organic frame to nitro-depleted nanopowders carbons: high CO2 uptake and efficient catalytic oxygen reduction[J].Journal of the American Chemical Society 2014,136:6790-6793]Reported that ZIF-8 is used as a templateAnd preparation of precursor Nitrogen doped porous carbon NC700 with 3.1 mmol. multidot.g at 273K and 1bar-1Adsorption amount of (2) and CO of 592/N2And (4) selectivity. Singh et al [ Singh D K, Krishna K S, Harish S, et al. No. more HF: teflon-assisted ultra removal of silicon to product high-surface-area structured carbon for Enhanced CO2 Capture and supercapacitor performance[J].Angewandte Chemie International Edition 2016,55:2032-2036]Reported as SiO2Ordered mesoporous carbon JCN-1 to CO prepared by template method2Adsorption amount and CO of2/N2IAST selectivities of 3.5 and 7 mmol-g, respectively-1
The applicant has found that although high adsorption capacity nitrogen doped porous carbon materials can be obtained by KOH activation, the randomness of the activation reaction results in carbon materials obtained by the method generally having a discrete pore size distribution, which in turn results in a lower effective utilization of the pore structure. In addition, the strong corrosiveness of KOH and the low yield of the activation method limit the practical application possibility. The precise synthesis of the sub-nanometer template in the template method is the biggest bottleneck of the application of the method. Therefore, the development of a safer and more efficient carbon-based adsorbent synthesis method has very important significance for gas adsorption separation engineering.
Disclosure of Invention
The invention aims to provide a method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method, and a method and application thereof. Effectively avoids the defects of corrosivity, poor safety, complex process and the like existing in the traditional activation method or template method, and the synthesized Co-NDPC is CH with great application prospect4/C2H2/C2H6/C3H8/CO2/N2Adsorbing the separating agent.
The purpose of the invention can be realized by the following technical scheme:
the invention provides a method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using an in-situ amorphous cobalt template method, wherein poly 4-vinylpyridine (P4VP) and cobalt chloride hexahydrate (CoCl)2·6H2O) as raw material, Co2+Form a thermally stable intermediate Co-P4VP with P4VP, in Co2+Under the catalytic action of the catalyst, P4VP in the Co-P4VP is converted into carbon nanosheet Co-NDC in the pyrolysis process, and Cl is introduced in the pyrolysis process-Inducing and Co-N bond confinement effect to induce the formation of amorphous Co nanoclusters, wrapping the amorphous Co nanoclusters in the P4VP converted carbon nanosheets, removing the amorphous Co nanoclusters through subsequent acid etching to form ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the diameters of 0.5 +/-0.05 nm, namely synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheets through the in-situ amorphous cobalt template method.
Preferably, the method comprises the steps of:
(a) mixing P4VP and CoCl2·6H2O is respectively dissolved in the solvent to obtain P4VP solution and CoCl2Solution, P4VP solution was added slowly to CoCl with stirring2Obtaining a mixed solution in the solution, and drying the mixed solution after vacuum rectification to obtain a thermal stability intermediate Co-P4 VP;
(b) carbonizing Co-P4VP in nitrogen atmosphere, and naturally cooling to room temperature to obtain carbon nanosheet Co-NDC;
(d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake to obtain the ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the pore diameter of 0.5 +/-0.05 nm, namely the nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method.
Preferably, in step (a), said P4VP is reacted with CoCl2·6H2The mass ratio of O is 0.1-1.0: 0.5 to 5.0; co in thermal stable intermediate Co-P4VP2+The atomic mol ratio of the solvent to the N is 2, and the solvent is absolute ethyl alcohol.
Preferably, in the step (b), the carbonization temperature is 500-900 ℃; the carbonization time is 2-4 h; the heating rate is 2.5-7.5 ℃ per minute-1
Preferably, in the step (c), the acid solution is 0.5-2.5M HCl solution, and the stirring time is 12-36 h.
Preferably, in the step (d), the drying temperature is 40-80 ℃ and the drying time is 12-36 h.
The invention provides a nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by an in-situ amorphous cobalt template method, and the nitrogen-doped monomodal ultramicropore carbon nanosheet is obtained by the method.
Preferably, the nitrogen-doped monomodal ultramicropore carbon nanosheet has a carbon nanosheet network structure, and the specific surface area is 500-1500 m2 g-1The volume of the micro-pores is 0.25-0.75 cm3·g-1The nitrogen doping amount is 3-15 at%, and the unimodal pore size distribution of 0.5 +/-0.05 nm is formed.
Further preferably, the nitrogen-doped monomodal ultramicropore carbon nanosheet has a unique carbon nanosheet network structure and a specific surface area of 900-1200 m2·g-1The micropore volume is 0.45-0.55 cm3·g-1The nitrogen doping amount is 10-12 at%, and the unimodal pore size distribution of 0.5 +/-0.05 nm is formed.
The third aspect of the invention provides application of the in-situ amorphous cobalt template method in synthesis of nitrogen-doped monomodal ultramicropore carbon nanosheets, and the nitrogen-doped monomodal ultramicropore carbon nanosheets are used as adsorbents for C2H2、C2H6、C3H8And CO2And has x/CH4And CO2/N2IAST selectivity, said x comprising C2H2、C2H6、C3H8Or CO2
Compared with the prior art, the invention has the following beneficial effects:
1. the invention introduces Co2+Form thermally stable intermediates Co-P4VPs with P4VP, in Co2+The P4VP in the Co-P4VPs can be converted into carbon and Co in the pyrolysis process2+Is critical to the carbon conversion of P4 VP. Furthermore, by Cl-Inducing and Co-N bond confinement effect to induce the formation of amorphous Co nanoclusters, coating the uniform ultra-small amorphous Co nanoclusters in the carbon nanosheets converted from P4VP, and removing the Co nanoclusters through a subsequent acid etching process to form ultra-micropores (approximately equal to 0.5nm) with uniform pore size. The invention avoids the defects of pore-forming by the traditional activation method and template method.
2. The nitrogen-doped unimodal ultramicropore carbon nano is synthesized by the in-situ amorphous cobalt template method prepared by the inventionThe rice flake (Co-NDPC) has a unique carbon nanosheet network structure and a high specific surface area (900-1200 m)2 g-1) The volume of the micro pores is 0.45-0.55 cm3·g-1High nitrogen doping amount (10-12 at%), unimodal pore size distribution (0.5 +/-0.05 nm) and the like. As adsorbent, at 298K and 1bar, Co-NDPC showed an ultra-high C2H2、C2H6、C3H8And CO2The adsorption capacities were 6.7, 5.9, 7.4 and 5.6 mmol/g, respectively-1Corresponding x/CH4(x=C2H2、C2H6、C3H8Or CO2). And CO2/N2The IAST selectivity is respectively as high as 75.3, 65.9, 1743.6, 11.4 and 74.7, and the method has high application value in the field of gas adsorption separation.
3. The invention effectively avoids the defects of corrosivity, poor safety, complex process and the like of the traditional activation method or template method, and the synthesized Co-NDPC is CH with great application prospect4/C2H2/C2H6/C3H8/CO2/N2Adsorbing the separating agent.
Drawings
FIG. 1 is a schematic diagram of the preparation of Co-NDPC according to the present invention;
FIG. 2 is a topographical feature of Co-NDPC-700 of the present invention: (a, b) SEM images; (c) SEM-mapping; (d-f) TEM images at different magnifications;
FIG. 3 is (a) Co-NDPC-500; (b) Co-NDPC-600; (c) Co-NDPC-800; (d) SEM image of Co-NDPC-900;
FIG. 4 shows (a) N of Co-NDPCs2Adsorption isotherms; (b) NLDFT pore size distribution curve.
Detailed Description
A method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using an in-situ amorphous cobalt template method is characterized in that poly-4-vinylpyridine (P4VP) and cobalt chloride hexahydrate (CoCl)2·6H2O) as raw material, Co2+Form a thermally stable intermediate Co-P4VP with P4VP, in Co2+Under the catalytic action of Co-P4VP, P4VP in the pyrolysis processIs converted into carbon nano-sheet Co-NDC, and is subjected to Cl passing in the pyrolysis process-Inducing and Co-N bond confinement effect to induce the formation of amorphous Co nanoclusters, wrapping the amorphous Co nanoclusters in the P4VP converted carbon nanosheets, removing the amorphous Co nanoclusters through subsequent acid etching to form ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the diameters of 0.5 +/-0.05 nm, namely synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheets through the in-situ amorphous cobalt template method.
More specifically, the method comprises the steps of:
(a) mixing P4VP and CoCl2·6H2O is respectively dissolved in the solvent to obtain P4VP solution and CoCl2Solution, P4VP solution was added slowly to CoCl with stirring2Obtaining a mixed solution in the solution, and drying the mixed solution after vacuum rectification to obtain a thermal stability intermediate Co-P4 VP;
(b) carbonizing Co-P4VP in nitrogen atmosphere, and naturally cooling to room temperature to obtain carbon nanosheet Co-NDC;
(d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake to obtain the ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the pore diameter of 0.5 +/-0.05 nm, namely the nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method.
In step (a), P4VP and CoCl are preferred2·6H2The mass ratio of O is 0.1-1.0: 0.5 to 5.0; co in thermal stable intermediate Co-P4VP2+The atomic mol ratio of the component to the component is 2, and the solvent is absolute ethyl alcohol.
In the step (b), the carbonization temperature is preferably 500-900 ℃; the carbonization time is 2-4 h; the heating rate is 2.5-7.5 ℃ per minute-1
In the step (c), the acid solution is preferably 0.5-2.5M HCl solution, and the stirring time is 12-36 h.
In the step (d), the drying temperature is preferably 40-80 ℃ and the time is 12-36 h.
The method for evaluating the gas adsorption separation performance comprises the following steps:
1. static adsorption Capacity test of samples at 0 and 25 deg.C
Sample pair CH at 0 and 25 ℃4、C2H2、C2H6、C3H8、CO2And N2The static adsorption test of (2) is characterized by an Autosorb-iQ2 specific surface area and a pore diameter adsorption instrument. The test range is 0-1 bar, the ice-water mixture is used as a test thermostat at 0 ℃, the water at 25 ℃ is used as a test thermostat at 25 ℃, and the mass of the sample is about 100 mg. The samples were degassed at 250 ℃ for 12h before testing.
Sample cycle stability was evaluated by conducting 5 consecutive adsorption-desorption experiments on an Autosorb-iQ2 adsorber. The sample was degassed just before the start of the first adsorption test and weighed at the end of each desorption to correct for the sample mass. The removal of gas between different cycles depends on the vacuum pumping process of the apparatus.
2. Adsorption data Single Point Langmuir-Freundlich model fitting
Figure BDA0002774282760000061
b is a temperature-related parameter, which is related as follows:
Figure BDA0002774282760000062
R=8.314J mol-1K-1.
3. gas adsorption selectivity prediction
The prediction of the adsorption selectivity (S) of the sample for different gases is calculated according to the Ideal Adsorption Solution Theory (IAST) and is calculated according to the following formula:
Figure BDA0002774282760000063
in the above formula xiAnd yiRepresents the molar fraction of i component (i ═ 1,2) in the adsorption and bulk phases, respectively, of the sample at adsorption equilibrium.
The invention is described in detail below with reference to the figures and specific embodiments.
Example 1
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to carbonization temperature of 500 ℃ in the atmosphere, preserving heat and carbonizing for 3h (heating rate of 5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-500, wherein 500 represents the carbonization temperature (DEG C); c) adding Co-NDC-500 into 200mL of 1M HCl solution, and magnetically stirring for 24h to remove metallic cobalt; d) washing the Co-NDC washed by the acid with deionized water to be neutral, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12h to obtain a final product named Co-NDPC-500, wherein 500 represents the carbonization temperature (DEG C). The nitrogen-doped single-peak ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method is subjected to structure characterization and gas adsorption separation performance test, and the results are shown in tables 1-4.
Example 2
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Under the atmosphereHeating to the carbonization temperature of 600 ℃, preserving heat and carbonizing for 3h (the heating rate is 5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-600, wherein 600 represents the carbonization temperature (DEG C); c) adding Co-NDC-600 into 200mL of 1M HCl solution, and magnetically stirring for 24h to remove metallic cobalt; d) washing the Co-NDC washed by the acid with deionized water to be neutral, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12h to obtain a final product, wherein 600 represents the carbonization temperature (DEG C). The nitrogen-doped single-peak ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method is subjected to structure characterization and gas adsorption separation performance test, and the results are shown in tables 1-4.
Example 3
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to 700 ℃ under the atmosphere, preserving heat and carbonizing for 3h (the heating rate is 5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-700, wherein 700 represents the carbonization temperature (DEG C); c) adding Co-NDC-700 into 200mL of 1M HCl solution, and magnetically stirring for 24h to remove metallic cobalt; d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12 hours to obtain a final product named Co-NDPC-700, wherein 700 represents the carbonization temperature (DEG C). The nitrogen-doped single-peak ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method is subjected to structure characterization and gas adsorption separation performance test, and the results are shown in tables 1-4.
Example 4
Nitrogen-doped single-peak ultramicropore synthesized by in-situ amorphous cobalt template methodA method for preparing carbon nano-sheets is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to the carbonization temperature of 800 ℃ in the atmosphere, preserving heat and carbonizing for 3h (the heating rate is 5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-800, wherein 800 represents the carbonization temperature (DEG C); c) adding Co-NDC-800 into 200mL of 1M HCl solution, and magnetically stirring for 24h to remove metallic cobalt; d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12 hours to obtain a final product named Co-NDPC-800, wherein 800 represents the carbonization temperature (DEG C). The nitrogen-doped single-peak ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method is subjected to structure characterization and gas adsorption separation performance test, and the results are shown in tables 1-4.
Example 5
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to 900 deg.C under atmosphere, and carbonizing for 3h (heating rate 5 deg.C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-900, wherein 900 represents the carbonization temperature (DEG C); c. C) Adding Co-NDC-900 into 200mL of 1M HCl solution, and magnetically stirring for 24 hours to remove metal cobalt; d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12 hours to obtain a final product named Co-NDPC-900, wherein 900 represents the carbonization temperature (DEG C). The nitrogen-doped single-peak ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method is subjected to structure characterization and gas adsorption separation performance test, and the results are shown in tables 1-4.
Example 6
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to the carbonization temperature of 700 ℃ in the atmosphere, preserving heat and carbonizing for 3h (the heating rate is 2.5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-700, wherein 700 represents the carbonization temperature (DEG C); c) adding Co-NDC-700 into 200mL of 1M HCl solution, and magnetically stirring for 24 hours to remove metal cobalt; d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12 hours to obtain a final product named Co-NDPC-700, wherein 700 represents the carbonization temperature (DEG C). And (3) synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheet by using an in-situ amorphous cobalt template method, and testing the gas adsorption separation performance.
Example 7
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2Dissolving O in 100mL of absolute ethanol respectively, and stirring to obtain P4 VP/ethylAlcohol solution was slowly added to CoCl2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to the carbonization temperature of 700 ℃ in the atmosphere, preserving heat and carbonizing for 3h (the heating rate is 7.5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-700, wherein 700 represents the carbonization temperature (DEG C); c) adding Co-NDC-700 into 200mL of 1M HCl solution, and magnetically stirring for 24 hours to remove metal cobalt; d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake in an oven at 60 ℃ for 12 hours to obtain a final product named Co-NDPC-700, wherein 700 represents the carbonization temperature (DEG C). And (3) synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheet by using an in-situ amorphous cobalt template method, and testing the gas adsorption separation performance.
Example 8
A preparation method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by an in-situ amorphous cobalt template method is characterized by comprising the following steps: a) 0.42g P4VP and 1.903g CoCl2·6H2O was dissolved in 100mL of absolute ethanol, and the P4 VP/ethanol solution was added slowly to CoCl with stirring2·6H2In O/ethanol solution, stirring for 4h by magnetic force to obtain P4VP/CoCl2Mixing the ethanol solution; the resulting P4VP/CoCl2Vacuum rectifying the ethanol mixed solution, and drying in an oven at 60 deg.C for 24h to obtain carbonized precursor Co-P4VP (Co)2+a/N atomic molar ratio of 2); b) placing the Co-P4VP precursor in a tube furnace, N2Heating to 700 ℃ under the atmosphere, preserving heat and carbonizing for 3h (the heating rate is 5 ℃ C. min)-1) Naturally cooling to room temperature to obtain a carbonization product Co-NDC-700, wherein 700 represents the carbonization temperature (DEG C); c) adding Co-NDC-700 into 200mL2.5M HCl solution, and magnetically stirring for 24h to remove metallic cobalt; d) washing the Co-NDC after acid washing with deionized water to neutrality, filtering to obtain a filter cake, drying the filter cake in an oven at 60 ℃ for 12h to obtain the final product named Co-NDPC-700, where 700 represents carbonization temperature (. degree. C.). And (3) synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheet by using an in-situ amorphous cobalt template method, and testing the gas adsorption separation performance.
TABLE 1 texture characteristics and metallic Co content of Co-NDPCs
Figure BDA0002774282760000101
The element content is as follows: (a) XPS (at%), (b) ICP-AES (wt%).
TABLE 2 examples gas loading at 273 or 298K, 1bar
Figure BDA0002774282760000102
TABLE 3 example at 298K, 1bar vs. x/CH4IAST selectivity of (50/50, v/v) binary gas mixture
Figure BDA0002774282760000111
TABLE 4 example at 298K, 1bar vs. CO2/N2(v/v) IAST Selectivity of binary gas mixture
Figure BDA0002774282760000112
The schematic diagram of the preparation process of Co-NDPC is shown in FIG. 1, and the morphological characteristics of Co-NDPC-700 in FIG. 2 are as follows: (a, b) SEM images; (c) SEM-mapping; (d-f) TEM image. FIG. 3(a) Co-NDPC-500; (b) Co-NDPC-600; (c) Co-NDPC-800; (d) SEM image of Co-NDPC-900. FIG. 4 shows (a) N of Co-NDPCs2Adsorption isotherms; (b) NLDFT pore size distribution curve.
In summary, as shown in FIGS. 1-4, tables 1-4, with P4VP and CoCl2·6H2O is taken as a raw material to successfully synthesize nitrogen-doped monomodal ultramicropore carbon nanosheets (Co-NDPC), and the Co-NDPC is prepared from Co2+And P4VP by carbonization, with Cl-Inducing and Co-N bond confinement effect to induce the formation of amorphous Co nanoclusters, coating the uniform ultra-small amorphous Co nanoclusters in the carbon nanosheets converted from P4VP, and removing the Co nanoclusters through a subsequent acid etching process to form ultra-micropores (approximately equal to 0.5nm) with uniform pore size. The Co-NDPC has a unique carbon nanosheet network structure and a high specific surface area (900-1200 m)2 g-1) The volume of the micro pores is 0.45-0.55 cm3·g-1High nitrogen doping amount (10-12 at%), unimodal pore size distribution (0.5 +/-0.05 nm) and the like. As adsorbent, at 298K and 1bar, Co-NDPC showed an ultra-high C2H2、C2H6、C3H8And CO2The adsorption capacities were 6.7, 5.9, 7.4 and 5.6 mmol/g, respectively-1Corresponding x/CH4And CO2/N2The IAST selectivity was also as high as 75.3, 65.9, 1743.6, 11.4, and 74.7, respectively. The synthesized Co-NDPC is CH with great application prospect4/C2H2/C2H6/C3H8/CO2/N2Adsorbing the separating agent.
The embodiments described above are intended to facilitate the understanding and use of the invention by those skilled in the art. It will be readily apparent to those skilled in the art that various modifications to these embodiments may be made, and the generic principles described herein may be applied to other embodiments without the use of the inventive faculty. Therefore, the present invention is not limited to the above embodiments, and those skilled in the art should make improvements and modifications within the scope of the present invention based on the disclosure of the present invention.

Claims (10)

1. The method for synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheet by using the in-situ amorphous cobalt template method is characterized in that P4VP and CoCl are used2·6H2O as a raw material, Co2+Form a thermally stable intermediate Co-P4VP with P4VP, in Co2+Under the catalytic action of the catalyst, P4VP in the Co-P4VP is converted into carbon nanosheet Co-NDC in the pyrolysis process, and Cl is introduced in the pyrolysis process-Induction and Co-N bond confinement effect induced amorphous Co nanoclusterForming clusters, enabling the clusters to be coated in the carbon nanosheets converted from P4VP, removing amorphous Co nanoclusters through subsequent acid etching, and forming ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the pore diameters of 0.5 +/-0.05 nm, namely synthesizing the nitrogen-doped monomodal ultramicropore carbon nanosheets through the in-situ amorphous cobalt template method.
2. The method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets according to claim 1, comprising the steps of:
(a) mixing P4VP and CoCl2·6H2O is respectively dissolved in the solvent to obtain P4VP solution and CoCl2Solution, P4VP solution was added slowly to CoCl with stirring2Obtaining a mixed solution in the solution, and drying the mixed solution after vacuum rectification to obtain a thermal stability intermediate Co-P4 VP;
(b) carbonizing Co-P4VP in nitrogen atmosphere, and naturally cooling to room temperature to obtain carbon nanosheet Co-NDC;
(c) adding Co-NDC into an acid solution, stirring, and removing metal cobalt in the solution;
(d) washing the Co-NDC subjected to acid washing with deionized water to neutrality, filtering to obtain a filter cake, and drying the filter cake to obtain the ultramicropore nitrogen-doped porous carbon Co-NDPC with ultramicropores with the pore diameter of 0.5 +/-0.05 nm, namely the nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by the in-situ amorphous cobalt template method.
3. The method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using in-situ amorphous cobalt templating method according to claim 2, wherein in step (a), P4VP and CoCl are used2·6H2The mass ratio of O is 0.1-1.0: 0.5 to 5.0; co in thermal stable intermediate Co-P4VP2+The atomic mol ratio of the solvent to the N is 2, and the solvent is absolute ethyl alcohol.
4. The method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using the in-situ amorphous cobalt template method according to claim 2, wherein in the step (b), the carbonization temperature is 500-900 ℃; carbon (C)The time for the reaction is 2-4 h; the heating rate is 2.5-7.5 ℃ per minute-1
5. The method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using the in-situ amorphous cobalt template method according to claim 2, wherein in step (c), the acid solution is 0.5-2.5M HCl solution, and the stirring time is 12-36 h.
6. The method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets by using the in-situ amorphous cobalt template method according to claim 2, wherein in step (d), the drying temperature is 40-80 ℃ and the drying time is 12-36 h.
7. An in-situ amorphous cobalt template method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheet, which is characterized by being obtained by the method of any one of claims 1 to 6.
8. The in-situ amorphous cobalt template method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets according to claim 7, wherein the nitrogen-doped monomodal ultramicropore carbon nanosheets have a carbon nanosheet network structure and a specific surface area of 500-1500 m2g-1The volume of the micro-pores is 0.25-0.75 cm3·g-1The nitrogen doping amount is 3-15 at%, and the unimodal pore size distribution of 0.5 +/-0.05 nm is formed.
9. The in-situ amorphous cobalt templating method of claim 8, wherein the nitrogen-doped unimodal nanoporous carbon nanoplatelets have a unique carbon nanoplatelet network structure with a specific surface area of 900-1200 m2·g-1The micropore volume is 0.45-0.55 cm3·g-1The nitrogen doping amount is 10-12 at%, and the unimodal pore size distribution of 0.5 +/-0.05 nm is formed.
10. Application of in-situ amorphous cobalt template method for synthesizing nitrogen-doped monomodal ultramicropore carbon nanosheets as claimed in any one of claims 7 to 9, wherein the nitrogen-doped monomodal ultramicropore carbon nanosheets are used as adsorbent for C2H2、C2H6、C3H8And CO2And has x/CH4And CO2/N2IAST selectivity, said x comprising C2H2、C2H6、C3H8Or CO2
CN202011259848.8A 2020-11-12 2020-11-12 Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof Pending CN112357906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011259848.8A CN112357906A (en) 2020-11-12 2020-11-12 Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011259848.8A CN112357906A (en) 2020-11-12 2020-11-12 Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof

Publications (1)

Publication Number Publication Date
CN112357906A true CN112357906A (en) 2021-02-12

Family

ID=74514487

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011259848.8A Pending CN112357906A (en) 2020-11-12 2020-11-12 Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof

Country Status (1)

Country Link
CN (1) CN112357906A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114410329A (en) * 2022-02-10 2022-04-29 山西沁新能源集团股份有限公司 High carbon coke with hybrid carbon and method for producing the same

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20100075087A (en) * 2008-12-24 2010-07-02 부산대학교 산학협력단 Nanoporous carbon with magnetic nanoparticles in nanopores and one-pot manufacturing method of the materials
CN103088465A (en) * 2011-10-28 2013-05-08 香港理工大学 Hollow graphite carbon nanometer sphere in-situ modification amorphous carbon nanometer fibers or carbon nano-tubes and preparation method thereof
CN105329874A (en) * 2014-08-08 2016-02-17 中国石油化工股份有限公司 Heteroatom-doped carbon microsphere and preparation method thereof
CN105439115A (en) * 2014-08-08 2016-03-30 中国石油化工股份有限公司 Heteroatom doping carbon nanoparticle and production method thereof
CN109179379A (en) * 2018-11-01 2019-01-11 中山大学 A kind of Specific surface area carbon material and its preparation method and application with carbon nanotube core@amorphous carbon shell unit
CN109942020A (en) * 2019-02-03 2019-06-28 复旦大学 A kind of preparation method of the three-dimensional network composite material of tubular metal oxide/carbon

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20100075087A (en) * 2008-12-24 2010-07-02 부산대학교 산학협력단 Nanoporous carbon with magnetic nanoparticles in nanopores and one-pot manufacturing method of the materials
CN103088465A (en) * 2011-10-28 2013-05-08 香港理工大学 Hollow graphite carbon nanometer sphere in-situ modification amorphous carbon nanometer fibers or carbon nano-tubes and preparation method thereof
CN105329874A (en) * 2014-08-08 2016-02-17 中国石油化工股份有限公司 Heteroatom-doped carbon microsphere and preparation method thereof
CN105439115A (en) * 2014-08-08 2016-03-30 中国石油化工股份有限公司 Heteroatom doping carbon nanoparticle and production method thereof
CN109179379A (en) * 2018-11-01 2019-01-11 中山大学 A kind of Specific surface area carbon material and its preparation method and application with carbon nanotube core@amorphous carbon shell unit
CN109942020A (en) * 2019-02-03 2019-06-28 复旦大学 A kind of preparation method of the three-dimensional network composite material of tubular metal oxide/carbon

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
NING FU ET AL.: "In-situ preparation of nitrogen-doped unimodal ultramicropore carbon nanosheets with ultrahigh gas selectivity", 《CARBON》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114410329A (en) * 2022-02-10 2022-04-29 山西沁新能源集团股份有限公司 High carbon coke with hybrid carbon and method for producing the same

Similar Documents

Publication Publication Date Title
Hu et al. Novel nanowire self-assembled hierarchical CeO2 microspheres for low temperature toluene catalytic combustion
He et al. Facile preparation of N-doped activated carbon produced from rice husk for CO2 capture
Chen et al. Nickel doping MnO2 with abundant surface pits as highly efficient catalysts for propane deep oxidation
Zhang et al. One-pot synthesis of carbonaceous monolith with surface sulfonic groups and its carbonization/activation
CN103372420B (en) The composite of metallic organic framework and amine-modified graphite oxide and preparation thereof
Ghasemy et al. N-doped CNT nanocatalyst prepared from camphor and urea for gas phase desulfurization: experimental and DFT study
Jin et al. Resource utilization of waste V2O5-based deNOx catalysts for hydrogen production from formaldehyde and water via steam reforming
Meng et al. MgO-templated porous carbons-based CO2 adsorbents produced by KOH activation
Jiménez et al. Hydrogen storage capacity on different carbon materials
CN106000405B (en) A kind of multi-stage porous loading type nickel-based catalyst, preparation method and application
Ma et al. Activity of microporous lignin-derived carbon-based solid catalysts used in biodiesel production
CN112279236A (en) Nitrogen-doped hollow carbon sphere and preparation method and application thereof
Wang et al. A synthesis of porous activated carbon materials derived from vitamin B9 base for CO2 capture and conversion
Shi et al. Biowaste-derived 3D honeycomb-like N and S dual-doped hierarchically porous carbons for high-efficient CO 2 capture
Fu et al. In-situ preparation of nitrogen-doped unimodal ultramicropore carbon nanosheets with ultrahigh gas selectivity
QUAN et al. Effect of preparation methods on the structure and catalytic performance of CeO2 for toluene combustion
Li et al. The effect of 3D carbon nanoadditives on lithium hydroxide monohydrate based composite materials for highly efficient low temperature thermochemical heat storage
Zhang et al. Catalytic performance of CH4–CO2 reforming over metal free nitrogen-doped biomass carbon catalysts: Effect of different preparation methods
Wang et al. Preparation of N-doped ordered mesoporous carbon and catalytic performance for the pyrolysis of 1-chloro-1, 1-difluoroethane to vinylidene fluoride
Kong et al. Ordered mesoporous carbon with enhanced porosity to support organic amines: efficient nanocomposites for the selective capture of CO 2
CN103933939A (en) Metal-organic framework MOF material with high methane adsorption and storage density
Zhang et al. Three-dimensional flower-like nickel phyllosilicates for CO 2 methanation: enhanced catalytic activity and high stability
CN112357906A (en) Nitrogen-doped monomodal ultramicropore carbon nanosheet synthesized by in-situ amorphous cobalt template method, and method and application thereof
Wang et al. Facile synthesis of MOF-5-derived porous carbon with adjustable pore size for CO2 capture
Lu et al. High nitrogen carbon material with rich defects as a highly efficient metal-free catalyst for excellent catalytic performance of acetylene hydrochlorination

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20210212

RJ01 Rejection of invention patent application after publication