CN106693899A - Metal organic framework material/functional ionic liquid composite material as well as preparation and application thereof - Google Patents

Metal organic framework material/functional ionic liquid composite material as well as preparation and application thereof Download PDF

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CN106693899A
CN106693899A CN201611116119.0A CN201611116119A CN106693899A CN 106693899 A CN106693899 A CN 106693899A CN 201611116119 A CN201611116119 A CN 201611116119A CN 106693899 A CN106693899 A CN 106693899A
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organic framework
metal
framework materials
liquid composite
preparation
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袁媛
于英豪
石卓
游高雄
杨婉欣
王乐夫
李雪辉
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South China University of Technology SCUT
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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
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • B01J20/226Coordination polymers, e.g. metal-organic frameworks [MOF], zeolitic imidazolate frameworks [ZIF]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0281Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member
    • B01J31/0284Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member of an aromatic ring, e.g. pyridinium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0285Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre also containing elements or functional groups covered by B01J31/0201 - B01J31/0274
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/1691Coordination polymers, e.g. metal-organic frameworks [MOF]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2204Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/2208Oxygen, e.g. acetylacetonates
    • B01J31/2213At least two complexing oxygen atoms present in an at least bidentate or bridging ligand
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/14Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including at least two different refining steps in the absence of hydrogen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/02Compositional aspects of complexes used, e.g. polynuclearity
    • B01J2531/0238Complexes comprising multidentate ligands, i.e. more than 2 ionic or coordinative bonds from the central metal to the ligand, the latter having at least two donor atoms, e.g. N, O, S, P
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/60Complexes comprising metals of Group VI (VIA or VIB) as the central metal
    • B01J2531/62Chromium

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  • Oil, Petroleum & Natural Gas (AREA)
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Abstract

The invention discloses a metal organic framework material/functional ionic liquid composite material as well as preparation and application thereof, and belongs to the technical field of light industry and chemical engineering materials. As a functional ionic liquid is synthesized and loaded on a meal organic framework material by using a 'ship-in-a-bottle synthesis' method, the circulation use efficiency of the ionic liquid can be effectively improved, and the use amount of the ionic liquid can be reduced; and due to the diversity of the metal organic framework material, a series of different metal organic framework materials/functional ionic liquid composite materials can be synthesized. The metal organic framework material/functional ionic liquid composite material disclosed by the invention can be applied to gasoline catalytic oxidation desulfurization, and the purposes of improving the catalytic property of a system, reducing the amount of the ionic liquid and facilitating product separation and catalyst recycling can be achieved. The composite material disclosed by the invention can be used as a catalyst for adsorbing, oxidizing, extracting and removing sulfur-containing substances in gasoline, and is gentle in reaction condition, good in desulfurization effect and easy in catalyst recycling.

Description

A kind of metal-organic framework materials/functionalized ion liquid composite and its preparation With application
Technical field
The invention belongs to light industry, the technical field of chemical materials, more particularly to a kind of metal-organic framework materials/function Change ionic liquid composite material and preparation method and application.
Background technology
With the fast development of global economy, the recoverable amount of Global Auto increases year by year, it is contemplated that various to the year two thousand fifty whole world The total recoverable amount of automobile will rise to 2,500,000,000 amounts.Automobile quantity is continuously increased, and to result in gasoline demand amount increase year by year.In gasoline The burning of sulfur-containing compound can produce oxysulfide (SOx), wherein SO2It is the main cause for causing acid rain.SO2Because it is soluble in Water, after respiratory tract is entered, major part is arrested in the upper respiratory tract, and generation has corrosive sulfurous on the mucous membrane of moistening Acid, sulfuric acid and sulfate, make stimulation stronger.And sulfur dioxide can also be rapidly absorbed into blood, produce poison secondary whole body Effect, the vigor of its energy destructive enzyme, there is certain infringement to liver.
Existence and life in order to avoid SOx on the mankind cause further influence, and countries in the world have been formulated one and have been in succession Strict standard is arranged to limit the content of sulfide in petrol.2008, the sulfur content of Japanese gasoline have decreased to 10mg/kg; European Union also came into effect Euro V emissions from 2009, it is desirable to which sulfur content is less than 10mg/kg in automobile-used petrol and diesel oil;In March, 2014 3, Environmental Protection Agency promulgated automobile emission and fuel oil quality new standard, new legislation specify sulfur content in gasoline from 30mg/kg is down to 10mg/kg.As can be seen here, the production low-sulfur even fuel oil without sulphur is the main trend of future world fuel oil development. In order to be integrated with the world, China has also made a series of strict sulfur-bearing standards in succession.On May 12nd, 2011, China's issue Motor petrol state IV standards, it is stipulated that vehicle gasoline and sulfur content in vehicle gasoline is less than 50mg/kg.Opened from 31 days zero May in 2012 Beijing Begin to carry out capital V motor petrol standards, normal benzine sulfur content is less than 10mg/kg.Due to China's oil Refining Technologies and developed country's phase Than also there is certain gap, therefore, comprehensive this target in line with international standards of sulfur content standard in gasoline is realized, task will more It is arduousness, therefore there is the deep desulfurization of gasoline technology of research and development economical and efficient highly important economic implications and society to anticipate Justice.Traditional hydrodesulfurization technology is to aromatics sulfide, and the removal effect of such as dibenzothiophenes and its derivative is bad.Be up to To the purpose of deep desulfuration, it is necessary to improve pressure and use noble metal catalyst, this necessarily increases operating cost and equipment investment.
At present, because its reaction condition is gentle, the equipment investment amount of money is few, desulfurized effect is good, especially for catalytic oxidation desulfurization There is selectivity well for the thiophene that is difficult to remove in hydrodesulfurization, dibenzothiophenes class organic sulfur, and be increasingly becoming Study hotspot.
The content of the invention
In order to overcome the shortcoming and deficiency of prior art, primary and foremost purpose of the invention is to provide a kind of metal organic framework The preparation method of material/functionalized ion liquid composite.Ionic liquid is existed by " ship construction method in bottle " specifically Synthesize and be limited in metal-organic framework materials in empty cage.
It is another object of the present invention to provide the metal-organic framework materials/function of being prepared by above-mentioned preparation method Change ionic liquid composite material.
It is yet a further object of the present invention to provide above-mentioned metal-organic framework materials/functionalized ion liquid composite Application.
The purpose of the present invention is achieved through the following technical solutions:
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite, comprises the following steps:
(1) inorganic salts and organic ligand are mixed, being subsequently adding stirring solvent dissolves it, insulation;Make after the completion of reaction It is cooled to room temperature, and washing precipitation is multiple, then filters, and is dried to obtain metal-organic framework materials;
(2) in the metal-organic framework materials input precursor A for obtaining step (1), stirring;Precursor B is subsequently adding, Continue to stir, then the ionic liquid H to being obtained2SO4Carry out ion exchange and obtain acidic ion liquid;Suction filtration, it is then right It is vacuum dried, so as to obtain metal-organic framework materials/functionalized ion liquid composite.
The cation of the inorganic salts described in step (1) is Cu2+、Zn2+、Zr4+、Cr3+、Fe3+And Al3+In at least one Kind;
The anion of the inorganic salts described in step (1) is NO3 -、Cl-And COO-In at least one.
Organic ligand described in step (1) is terephthalic acid (TPA) (a), trimesic acid (b), 2,6- naphthalenedicarboxylic acids (c), At least one in 2,4,6- tri- (4- carboxyl phenyls) -1,3,5-triazines (d), its structural formula is
Solvent described in step (1) is N,N-dimethylformamide (DMF), N, N- DEFs (DEF), second At least one in alcohol, hydrofluoric acid (HF) and water.
The cation of the inorganic salts described in step (1) is 8 with the mol ratio of organic ligand:25~15:1, solvent Consumption is 40~60mL;
The condition of the insulation described in step (1) is 85~220 DEG C of 8~48h of insulation;
Dry condition described in step (1) is 80~200 DEG C of 12~15h of drying;
Precursor A described in step (2) is N- methylimidazoles.
Precursor B described in step (2) is n-Propyl Bromide or 1,3- propane sultones.
The condition of the stirring described in step (2) is to stir 15h at room temperature;
The condition that continuation described in step (2) is stirred is 60 DEG C of stirring 24h;
Precursor A and the mol ratio of precursor B described in step (2) are 1:1~1:2;Preferably 1:1.2.
Vacuum drying condition described in step (2) is 80 DEG C of vacuum drying 24h;
A kind of metal-organic framework materials/functionalized ion liquid composite, are prepared by above-mentioned preparation method.
Described metal-organic framework materials/application of the functionalized ion liquid composite in gasoline desulfurization.
The application is with metal-organic framework materials/functionalized ion liquid composite as catalyst and adsorbent, With H2O2It is oxidant, with acetonitrile as extractant, the sulfide in gasoline is removed by the coupled modes of adsorbing-oxidising-extraction.
The present invention has the following advantages and effect relative to prior art:
(1) functionalized ion liquid is synthesized and is supported on metal-organic framework materials by the present invention using " ship construction method in bottle " On, the recycling efficiency of ionic liquid and the consumption of reduction ionic liquid can be effectively improved;
(2) present invention can synthesize a series of organic bones of different metals due to the diversity of metal-organic framework materials Frame material/functionalized ion liquid composite.
(3) metal-organic framework materials/functionalized ion liquid composite that the present invention is obtained is used for gasoline catalyzing oxygen Change desulfurization, reach raising system catalytic performance, the mesh for reducing ionic liquid consumption, being easy to product separation and catalyst recycle 's.
(4) composite that the present invention is obtained is used for sulfur-bearing thing in adsorbing-oxidising-extraction removing gasoline as catalyst Matter, its reaction condition is gentle, desulfurized effect is good, catalyst is easily reclaimed.
Specific embodiment
With reference to embodiment, the present invention is described in further detail, but embodiments of the present invention not limited to this.
Embodiment 1
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite is present embodiments provided, The preparation method specifically includes following steps:
(1) 60mL distilled water is added in the reactor of polytetrafluoroethyllining lining first, is subsequently adding 5.00g (12.5mmol)Cr(NO3)3·9H2O and 2.08g (12.5mmol) terephthalic acid (TPA), stir 20min, are eventually adding 0.63g HF (40%), 220 DEG C of heating 8h, are cooled to room temperature, are filtrated to get green solid.Solid is washed with DMF, ethanol, will finally be obtained Solid dried one the whole night at 150 DEG C, obtain MIL-101 (Cr).
(2) toward addition 0.5g MIL-101 (Cr) in 50mL flasks, 4.106g (0.05mol) N- methylimidazoles, room are added The lower stirring 15h of temperature.Add 7.3795g (0.06mol) n-Propyl Bromide, 60 DEG C of stirring 24h.Suction filtration, washes three times, every time with ethanol Resulting solid is added 20mL ethanol by 10mL, adds excessive H2SO4, 24h is stirred at room temperature, filter, washing, 80 DEG C are true Sky dries 24h, finally obtains metal-organic framework materials/functionalized ion liquid composite, as catalyst A:[PMIm] HSO4@MIL-101(Cr)。
Dibenzothiophenes is dissolved in normal octane by the dibenzothiophenes of more difficult removing as target sulphide with hydrodesulfurization, It is configured to the analog gasoline that sulfur content is 50ppm.Analog gasoline 10mL is taken, catalyst A0.06g mixes with analog gasoline.Add Hydrogen peroxide and 10mL acetonitriles, with hydrogen peroxide as oxidant, acetonitrile is added to the mixed liquor of fuel gasoline and catalyst for extractant In, at a temperature of 60 DEG C, 2h being stirred, the mol ratio of the S in O and analog gasoline in hydrogen peroxide is 50.Stratification after suction filtration, It is 9ppm to take upper strata analog gasoline high performance liquid chromatography and determine sulfur content, and desulfurization degree reaches 82%.
Embodiment 2
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite is present embodiments provided, The preparation method specifically includes following steps:
(1) 60mL DMF are added in the reactor of polytetrafluoroethyllining lining first, are subsequently adding 1.75g ZrCl4 (7.5mmol) and 1.25g (7.5mmol) terephthalic acid (TPA), stirs 20min, dissolves it, 120 DEG C of heating 24h, is cooled to room Temperature, is filtrated to get solid.Solid is washed with DMF, methyl alcohol, the solid that will finally obtain dries one the whole night at 80 DEG C, obtains UiO-66。
(2) toward addition 0.5g UiO-66 in 50mL flasks, 4.106g (0.05mol) N- methylimidazoles are added, is stirred at room temperature Mix 15h.Add 7.3795g (0.06mol) n-Propyl Bromide, 60 DEG C of stirring 24h.Suction filtration, is washed three times, each 10mL with ethanol. Resulting solid is added into 20mL ethanol, excessive H is added2SO4, 24h is stirred at room temperature, filter, washing, 80 DEG C of vacuum are done Dry 24h, finally obtains metal-organic framework materials/functionalized ion liquid composite, as catalyst B:[PMIm]HSO4@ UiO-66。
Dibenzothiophenes is dissolved in normal octane by the dibenzothiophenes of more difficult removing as target sulphide with hydrodesulfurization, It is configured to the analog gasoline that sulfur content is 50ppm.Analog gasoline 10mL is taken, catalyst B 0.06g mix with analog gasoline.Add Hydrogen peroxide and 10mL acetonitriles, with hydrogen peroxide as oxidant, acetonitrile is added to the mixed liquor of fuel gasoline and catalyst for extractant In, at a temperature of 60 DEG C, 2h being stirred, the mol ratio of the S in O and analog gasoline in hydrogen peroxide is 50.Stratification after suction filtration, It is 7.5ppm to take upper strata analog gasoline high performance liquid chromatography and determine sulfur content, and desulfurization degree reaches 85%.
Embodiment 3
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite is present embodiments provided, The preparation method specifically includes following steps:
(1) 50mL DEF are added in the reactor of polytetrafluoroethyllining lining first, are subsequently adding 0.6g Zn (NO3)2(3.2mmol) and 2.20g (10mmol) NDA, stirs 20min, dissolves it, 95 DEG C of heating 12h, cooling To room temperature, solid is filtrated to get.Solid is washed with DEF, the solid that will finally obtain dries one the whole night at 200 DEG C, obtains IRMOF-8。
(2) toward addition 0.5g IRMOF-8 in 50mL flasks, 4.106g (0.05mol) N- methylimidazoles are added, at room temperature Stirring 15h.Add 7.3795g (0.06mol) n-Propyl Bromide, 60 DEG C of stirring 24h.Suction filtration, washes three times, every time with ethanol 10mL.Resulting solid is added into 20mL ethanol, excessive H is added2SO4, 24h is stirred at room temperature, filter, washing, 80 DEG C are true Sky dries 24h, finally obtains metal-organic framework materials/functionalized ion liquid composite, as catalyst C:[PMIm] HSO4@IRMOF-8。
Dibenzothiophenes is dissolved in normal octane by the dibenzothiophenes of more difficult removing as target sulphide with hydrodesulfurization, It is configured to the analog gasoline that sulfur content is 50ppm.Analog gasoline 10mL is taken, catalyst C 0.06g mix with analog gasoline.Add Hydrogen peroxide and 10mL acetonitriles, with hydrogen peroxide as oxidant, acetonitrile is added to the mixed liquor of fuel gasoline and catalyst for extractant In, at a temperature of 60 DEG C, 2h being stirred, the mol ratio of the S in O and analog gasoline in hydrogen peroxide is 50.Stratification after suction filtration, It is 10ppm to take upper strata analog gasoline high performance liquid chromatography and determine sulfur content, and desulfurization degree reaches 80%.
Embodiment 4
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite is present embodiments provided, The preparation method specifically includes following steps:
(1) 40mL DMF are added in the reactor of polytetrafluoroethyllining lining first, are subsequently adding 2.90g Cu (NO3)2·3H2O (12mmol) and 0.35g (0.8mmol) 2,4,6- tri- (4- carboxyl phenyls) -1,3,5-triazines, stir 20min, Dissolve it, 85 DEG C of heating 48h are cooled to room temperature, are filtrated to get solid.Solid is washed with DMF, the solid that will finally obtain exists One is dried at 80 DEG C the whole night, PCN-6 is obtained.
(2) toward addition 0.5g PCN-6 in 50mL flasks, 4.106g (0.05mol) N- methylimidazoles are added, is stirred at room temperature Mix 15h.Add 7.3795g (0.06mol) n-Propyl Bromide, 60 DEG C of stirring 24h.Suction filtration, is washed three times, each 10mL with ethanol. Resulting solid is added into 20mL ethanol, a certain amount of H is added2SO4, 24h is stirred at room temperature, filter, washing, 80 DEG C of vacuum 24h is dried, metal-organic framework materials/functionalized ion liquid composite, as catalyst D is finally obtained:[PMIm] HSO4@PCN-6。
Dibenzothiophenes is dissolved in normal octane by the dibenzothiophenes of more difficult removing as target sulphide with hydrodesulfurization, It is configured to the analog gasoline that sulfur content is 50ppm.Analog gasoline 10mL is taken, catalyst D 0.06g mix with analog gasoline.Add Hydrogen peroxide and 10mL acetonitriles, with hydrogen peroxide as oxidant, acetonitrile is added to the mixed liquor of fuel gasoline and catalyst for extractant In, at a temperature of 60 DEG C, 2h being stirred, the mol ratio of the S in O and analog gasoline in hydrogen peroxide is 50.Stratification after suction filtration, It is 8.5ppm to take upper strata analog gasoline high performance liquid chromatography and determine sulfur content, and desulfurization degree reaches 83%.
Embodiment 5
A kind of preparation method of metal-organic framework materials/functionalized ion liquid composite is present embodiments provided, The preparation method specifically includes following steps:
(1) 60mL distilled water is added in the reactor of polytetrafluoroethyllining lining first, is subsequently adding 5.00g (12.5mmol)Cr(NO3)3·9H2O and 2.08g (12.5mmol) terephthalic acid (TPA), stir 20min, are eventually adding 0.63g HF (40%), 220 DEG C of heating 8h, are cooled to room temperature, are filtrated to get green solid.Solid is washed with DMF, ethanol, will finally be obtained Solid dried one the whole night at 150 DEG C, obtain MIL-101 (Cr).
(2) toward addition 0.5g MIL-101 (Cr) in 50mL flasks, 4.106g (0.05mol) N- methylimidazoles, room are added The lower stirring 15h of temperature.Add 7.3284g (0.06mol) PS, 60 DEG C of stirring 24h.Suction filtration, three are washed with ethanol It is secondary, each 10mL.Resulting solid is added into 20mL ethanol, excessive H is added2SO4, 24h is stirred at room temperature, filter, wash Wash, 80 DEG C of vacuum drying 24h finally obtain metal-organic framework materials/functionalized ion liquid composite, as catalyst E:[BSO3PMIm]HSO4@MIL-101(Cr)。
Dibenzothiophenes is dissolved in normal octane by the dibenzothiophenes of more difficult removing as target sulphide with hydrodesulfurization, It is configured to the analog gasoline that sulfur content is 50ppm.Analog gasoline 10mL is taken, catalyst E 0.06g mix with analog gasoline.Add Hydrogen peroxide and 10mL acetonitriles, with hydrogen peroxide as oxidant, acetonitrile is added to the mixed liquor of fuel gasoline and catalyst for extractant In, at a temperature of 60 DEG C, 2h being stirred, the mol ratio of the S in O and analog gasoline in hydrogen peroxide is 50.Stratification after suction filtration, It is 4.5ppm to take upper strata analog gasoline high performance liquid chromatography and determine sulfur content, and desulfurization degree reaches 91%.
Above-described embodiment is the present invention preferably implementation method, but embodiments of the present invention are not by above-described embodiment Limitation, it is other it is any without departing from Spirit Essence of the invention and the change, modification, replacement made under principle, combine, simplification, Equivalent substitute mode is should be, is included within protection scope of the present invention.

Claims (10)

1. the preparation method of a kind of metal-organic framework materials/functionalized ion liquid composite, it is characterised in that including with Lower step:
(1) inorganic salts and organic ligand are mixed, being subsequently adding stirring solvent dissolves it, insulation;Make its cold after the completion of reaction But room temperature is arrived, washing precipitation is multiple, then filters, and is dried to obtain metal-organic framework materials;
(2) in the metal-organic framework materials input precursor A for obtaining step (1), stirring;Precursor B is subsequently adding, is continued Stir, then the ionic liquid H to being obtained2SO4Carry out ion exchange and obtain acidic ion liquid;Suction filtration, then enters to it Row vacuum drying, so as to obtain metal-organic framework materials/functionalized ion liquid composite.
2. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
The cation of the inorganic salts described in step (1) is Cu2+、Zn2+、Zr4+、Cr3+、Fe3+And Al3+In at least one;
The anion of the inorganic salts described in step (1) is NO3 -、Cl-And COO-In at least one.
3. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
Organic ligand described in step (1) is terephthalic acid (TPA), trimesic acid, 2,6- naphthalenedicarboxylic acids, (the 4- carboxylics of 2,4,6- tri- Base phenyl) at least one in -1,3,5- triazines.
4. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
Solvent described in step (1) is N,N-dimethylformamide, N, in N- DEFs, ethanol, hydrofluoric acid and water At least one.
5. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
The cation of the inorganic salts described in step (1) is 8 with the mol ratio of organic ligand:25~15:1, the consumption of solvent It is 40~60mL.
6. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
The condition of the insulation described in step (1) is 85~220 DEG C of 8~48h of insulation;
Dry condition described in step (1) is 80~200 DEG C of 12~15h of drying.
7. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
Precursor A described in step (2) is N- methylimidazoles;
Precursor B described in step (2) is n-Propyl Bromide or 1,3- propane sultones.
8. the preparation method of metal-organic framework materials according to claim 1/functionalized ion liquid composite, its It is characterised by:
Precursor A and the mol ratio of precursor B described in step (2) are 1:1~1:2.
9. a kind of metal-organic framework materials/functionalized ion liquid composite, it is characterised in that by claim 1~8 Preparation method described in any one is prepared.
10. the metal-organic framework materials described in claim 9/functionalized ion liquid composite in gasoline desulfurization should With.
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107857886A (en) * 2017-11-21 2018-03-30 江南大学 A kind of Zr MOF preparation method
CN108435254A (en) * 2018-03-20 2018-08-24 华南理工大学 A kind of acidic ion liquid gasoline desulphurization catalyst and the preparation method and application thereof
CN109603911A (en) * 2018-12-29 2019-04-12 华南理工大学 A kind of functionalized ion liquid/zeolite imidazole ester skeletal composite and its preparation method and application
CN110041533A (en) * 2019-05-29 2019-07-23 福州大学 A kind of method that ionic liquid ligand displacement method prepares functional metal organic framework material
CN110331001A (en) * 2019-07-11 2019-10-15 福建师范大学福清分校 The preparation method and applications of the immobilized ionic liquid of ferrous metals organic backbone
CN110496608A (en) * 2019-08-13 2019-11-26 辽宁大学 A kind of poly ion liquid@metal organic framework composite material xPILs@MIL-101 and its preparation method and application
CN110911735A (en) * 2019-11-05 2020-03-24 华中科技大学 Quasi-solid electrolyte for lithium metal battery and preparation method thereof
CN110918124A (en) * 2019-12-12 2020-03-27 福建师范大学福清分校 Preparation method and application of iron-based MOFs immobilized ionic liquid
CN113926304A (en) * 2021-03-22 2022-01-14 青岛大学 Low-temperature demercuration adsorbent for coal-fired flue gas
CN114539550A (en) * 2022-03-16 2022-05-27 江苏大学 Third-class porous ionic liquid based on UiO-66 and preparation method and application thereof
CN114573854A (en) * 2022-03-16 2022-06-03 江苏大学 Preparation method of quaternary phosphonium third porous ionic liquid
CN114588879A (en) * 2022-03-31 2022-06-07 北京化工大学 IL @ MOFs composite material and preparation method and application thereof
CN115805100A (en) * 2021-09-13 2023-03-17 中国石油化工股份有限公司 Organic metal catalyst and preparation method and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102824895A (en) * 2012-08-31 2012-12-19 华南理工大学 Mesoporous limited functionalized ionic liquid composite material and preparation method and application thereof
CN103920158A (en) * 2014-04-24 2014-07-16 青岛大学 Chitosan-functionalized metal organic framework materials as well as preparation method and application thereof
CN104370820A (en) * 2013-08-13 2015-02-25 中国科学院大连化学物理研究所 Preparation method and applications of porous metal organic skeleton material
CN105327689A (en) * 2015-10-16 2016-02-17 华南理工大学 Preparation and applications of molecular sieve gasoline desulfurizing agent loaded with functionalized ionic liquid
WO2016168092A1 (en) * 2015-04-11 2016-10-20 Northwestern University Metal-organic frameworks for adsorption of liquid phase compounds

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102824895A (en) * 2012-08-31 2012-12-19 华南理工大学 Mesoporous limited functionalized ionic liquid composite material and preparation method and application thereof
CN104370820A (en) * 2013-08-13 2015-02-25 中国科学院大连化学物理研究所 Preparation method and applications of porous metal organic skeleton material
CN103920158A (en) * 2014-04-24 2014-07-16 青岛大学 Chitosan-functionalized metal organic framework materials as well as preparation method and application thereof
WO2016168092A1 (en) * 2015-04-11 2016-10-20 Northwestern University Metal-organic frameworks for adsorption of liquid phase compounds
CN105327689A (en) * 2015-10-16 2016-02-17 华南理工大学 Preparation and applications of molecular sieve gasoline desulfurizing agent loaded with functionalized ionic liquid

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张欢: "金属有机骨架材料对汽油馏分的吸附脱硫", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107857886A (en) * 2017-11-21 2018-03-30 江南大学 A kind of Zr MOF preparation method
CN108435254A (en) * 2018-03-20 2018-08-24 华南理工大学 A kind of acidic ion liquid gasoline desulphurization catalyst and the preparation method and application thereof
CN109603911A (en) * 2018-12-29 2019-04-12 华南理工大学 A kind of functionalized ion liquid/zeolite imidazole ester skeletal composite and its preparation method and application
CN110041533B (en) * 2019-05-29 2020-08-11 福州大学 Method for preparing functionalized metal organic framework material by ionic liquid ligand displacement method
CN110041533A (en) * 2019-05-29 2019-07-23 福州大学 A kind of method that ionic liquid ligand displacement method prepares functional metal organic framework material
CN110331001A (en) * 2019-07-11 2019-10-15 福建师范大学福清分校 The preparation method and applications of the immobilized ionic liquid of ferrous metals organic backbone
CN110496608A (en) * 2019-08-13 2019-11-26 辽宁大学 A kind of poly ion liquid@metal organic framework composite material xPILs@MIL-101 and its preparation method and application
CN110911735A (en) * 2019-11-05 2020-03-24 华中科技大学 Quasi-solid electrolyte for lithium metal battery and preparation method thereof
CN110918124A (en) * 2019-12-12 2020-03-27 福建师范大学福清分校 Preparation method and application of iron-based MOFs immobilized ionic liquid
CN113926304A (en) * 2021-03-22 2022-01-14 青岛大学 Low-temperature demercuration adsorbent for coal-fired flue gas
CN113926304B (en) * 2021-03-22 2024-01-16 青岛大学 Low-temperature mercury-removing adsorbent for coal-fired flue gas
CN115805100A (en) * 2021-09-13 2023-03-17 中国石油化工股份有限公司 Organic metal catalyst and preparation method and application thereof
CN115805100B (en) * 2021-09-13 2024-05-28 中国石油化工股份有限公司 Organometallic catalyst and preparation method and application thereof
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CN114573854B (en) * 2022-03-16 2023-08-04 江苏大学 Preparation method of quaternary phosphonium third-class porous ionic liquid
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CN114588879B (en) * 2022-03-31 2023-11-17 北京化工大学 IL@MOFs composite material and preparation method and application thereof

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