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A kind of preparation method and application of ionic liquid and metal organic framework composite adsorbent

A technology of metal-organic frameworks and ionic liquids, which is applied in separation methods, chemical instruments and methods, and separation of dispersed particles. It can solve the problems of limiting the industrial application of ionic liquids, high viscosity of ionic liquids, and high energy consumption for desorption and regeneration. It can be designed Strong resistance, high hydrothermal stability and acid and alkali resistance, and the effect of improving selectivity

Active Publication Date: 2021-03-05
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although ionic liquids have a good potential for absorbing and separating ethylene acetylene, and for industrial applications, the absorption capacity is also an important parameter related to the amount of absorbent and the economic benefits of the process, the absorption capacity of acetylene synthesized by existing designs is still small , limiting the industrial application of ionic liquids
At the same time, when ionic liquids are used in the absorption and separation of ethylene acetylene, it is inevitable to encounter problems such as large amount of ionic liquids and high energy consumption for desorption and regeneration; and the high viscosity of ionic liquids greatly reduces its absorption efficiency.

Method used

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  • A kind of preparation method and application of ionic liquid and metal organic framework composite adsorbent
  • A kind of preparation method and application of ionic liquid and metal organic framework composite adsorbent
  • A kind of preparation method and application of ionic liquid and metal organic framework composite adsorbent

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] MIL-101 can be prepared according to the existing published literature methods, specifically: add 4.00g of chromium nitrate nonahydrate, 1.64g of terephthalic acid, 125μL of hydrofluoric acid and 70mL of water into a 100mL reaction kettle, and sonicate for 3h. React at 220°C for 8 hours to obtain unpurified MIL-101 crystals. After cooling, the unpurified MIL-101 was sequentially treated with hot water at 80°C for 5h, hot ethanol at 60°C for 3h, ammonium fluoride at 60°C for 10h, and finally washed with hot water ultrasonically for 5 times. It is to remove the terephthalic acid ligand remaining in the channel. The purified product was vacuum-dried at 80°C and 150°C for 12h and 5h, respectively, to obtain the purified MIL-101 as a green solid powder. The specific surface area is 3000m 2 / g, the pore volume is 1.5cm 3 / g(P / P 0 = 0.95). Unless otherwise specified, the following examples are MIL-101 synthesized by this method.

[0044] After testing, at 298K, under 100...

Embodiment 2

[0046] Preparation of the adsorbent [Bmim][OAc]@MIL-101: Accurately weigh 0.5500g of [Bmim][OAc] and dissolve it in 5mL of chromatographically pure ethanol. in ethanol. Then, 150 mg of purified MIL-101 was added to the above solution, and the stirring was continued for 24 h. Green solid powder was obtained by suction filtration, and vacuum-dried at 80°C for 12 hours to obtain [Bmim][OAc]@MIL-101 with a loading capacity of 1.0 mmol / g.

[0047] After testing, at 298K and 100kPa, the adsorption capacity of the adsorbent prepared in this example is 2.0mmol / g for acetylene, and 0.84mmol / g for ethylene, and IAST calculates C 2 h 2 / C 2 h 4 (1:1) separation selectivity is 6.7; at 273K, 100kPa, the adsorption capacity of acetylene is 3.0mmol / g, the adsorption capacity of ethylene is 1.5mmol / g, IAST calculation C 2 h 2 / C 2 h 4 (1:1) separation selectivity was 7.9.

Embodiment 3

[0049] Preparation of adsorbent [Bmim][OAc]@MIL-101: Accurately weigh 0.0500g of [Bmim][OAc] and dissolve it in 5mL of chromatographically pure ethanol. in ethanol. Then, 150 mg of purified MIL-101 was added to the above solution, and the stirring was continued for 24 h. Green solid powder was obtained by suction filtration, and vacuum-dried at 80°C for 12 hours to obtain [Bmim][OAc]@MIL-101 with a loading capacity of 0.1 mmol / g.

[0050] After testing, at 298K and 100kPa, the adsorption capacity of the adsorbent prepared in this example is 2.5mmol / g for acetylene and 1.3mmol / g for ethylene, and IAST calculates C 2 h 2 / C 2 h 4 (1:1) separation selectivity is 3.2; at 273K, 100kPa, the adsorption capacity of acetylene is 4.1mmol / g, the adsorption capacity of ethylene is 2.3mmol / g, IAST calculation C 2 h 2 / C 2 h 4 (1:1) separation selectivity was 3.7.

[0051] figure 1 It is the XRD characterization diagram of MIL-101 prepared in Example 1 and [Bmim][OAc]@MIL-101 prep...

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Abstract

The invention discloses an ionic liquid and metal organic framework composite adsorbent and a preparation method and application thereof. A stable metal organic framework material is used as a carrier, ionic liquid is used as an active component, and various ionic liquids are adsorbed by surface adsorption. It is loaded into the pores of the metal organic framework material, and the loading amount is 0.05-3.0 mmol / g. The invention also discloses a preparation method of the adsorbent, which includes preparing various metal-organic framework materials MIL-101, UiO-66, HKUST-1, etc., and then mixing the metal-organic framework materials with the alcohol solution of the ionic liquid, and adsorbing loaded to obtain the adsorbent IL@MOF. The preparation process is simple and the conditions are mild, and the prepared adsorbent can realize high selective separation of olefin / alkyne mixed gas.

Description

technical field [0001] The invention relates to the technical field of adsorption materials and energy, in particular to a preparation method of an ionic liquid and a metal-organic framework composite adsorbent and its application in the separation of alkenes and alkynes. Background technique [0002] As one of the most important chemical raw materials, olefins are widely used in the production of lubricants, plastics, polymers and other chemical materials, among which ethylene is known as the "mother of the petrochemical industry". At present, olefins are mainly obtained through the cracking of petroleum, natural gas and multi-carbon hydrocarbons, but the cracking products are relatively complex, often containing a variety of alkanes, monoolefins, dienes, alkynes, diynes, etc. with different carbon numbers. Industrial applications often require high purity polymer grade olefins. For example, in the production of polyethylene, if there is a small amount of acetylene residue...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/22B01J20/30B01D53/02
Inventor 鲍宗必王佳伟任其龙邢华斌杨启炜张治国杨亦文苏宝根
Owner ZHEJIANG UNIV