A preparation method of pervaporation layer-by-layer assembly membrane for gasoline desulfurization

A technology of pervaporation membrane and layer-by-layer assembly, which is applied in the fields of dialysis purification, chemical instruments and methods, and semi-permeable membrane separation, etc. Problems such as the increase of molecular mass transfer resistance, to achieve the effect of improving structure and performance stability, good industrial application prospects, and strong adsorption selection ability

Active Publication Date: 2021-10-26
BEIJING TECHNOLOGY AND BUSINESS UNIVERSITY
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the significant difference in physical and chemical properties between inorganic particles and PEG polymer membrane materials, there are two important challenges in the preparation process of inorganic particle-filled PEG mixed matrix membranes. It is easy to form non-selective defects, which cannot exert the modification effect of inorganic particles on polymer membranes, and instead causes a decrease in the selectivity of membranes for small molecules. Therefore, researchers often use methods of increasing the thickness of mixed matrix membranes to weaken non-selective The selectivity decline caused by sexual defects, which also caused the increase of mass transfer resistance of small molecules, and the decrease of permeation flux; When the interaction force between the material-based film and the inorganic particles is too weak, it is easy to cause interface defects, resulting in a decrease in selectivity. If the interaction between the two is strong, the PEG molecular chain enters the pores of the inorganic particles in the presence of a solvent, which may block some The pores of inorganic particles make it difficult to give full play to the preferential adsorption of sulfur by inorganic particles, resulting in a low sulfur-enrichment factor. Therefore, designing and preparing inorganic particles with better compatibility with PEG-based membranes is also the key to improving their separation performance.

Method used

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  • A preparation method of pervaporation layer-by-layer assembly membrane for gasoline desulfurization
  • A preparation method of pervaporation layer-by-layer assembly membrane for gasoline desulfurization
  • A preparation method of pervaporation layer-by-layer assembly membrane for gasoline desulfurization

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Embodiment 1

[0023] 1) Preparation of porous bottom membrane: mix polymer bottom membrane material PVDF, inorganic particle zinc nitrate, and solvent triethyl phosphate, stir at 90°C for 2 hours until the membrane liquid is uniform, and then place it in a vacuum oven for defoaming to obtain inorganic Particle / polymer film liquid; the mass ratio of polymer base film material, inorganic particles, and solvent is 100:0.5:300; the obtained film liquid is coated with a scraping film on polyester non-woven fabric, and water is used as a gel bath , using the immersion precipitation phase inversion method to make the membrane, so that the solvent and water in the membrane liquid can be exchanged thoroughly;

[0024]2) In-situ preparation of MOFs membrane: dissolve the organic ligand 2-methylimidazole and the metal salt zinc nitrate in the solvent methanol, mix well, and immerse the bottom membrane prepared in step 1) into the organic ligand and metal salt 10s in the mixed solution, the temperature...

Embodiment 2

[0028] 1) Preparation of porous bottom membrane: mix polymer bottom membrane material PEI, inorganic particle zinc nitrate, and solvent N-methylpyrrolidone, stir at 80°C for 12 hours until the membrane liquid is uniform, and then place it in a vacuum oven for degassing to obtain Inorganic particles / polymer film liquid; the mass ratio of polymer bottom film material, inorganic particles, and solvent is 100:5:500; the obtained film liquid is coated with scraping film on polyester non-woven fabric, and water is used as gel Bath, the membrane is prepared by the immersion precipitation phase inversion method, so that the solvent and water in the membrane liquid can be exchanged thoroughly;

[0029] 2) In-situ preparation of MOFs membrane: Dissolve the organic ligand benzimidazole and the metal salt zinc nitrate in the solvent ethanol, mix well, and immerse the bottom membrane prepared in step 1) into the mixture containing the organic ligand and the metal salt. In the solution for ...

Embodiment 3

[0033] 1) Preparation of porous bottom membrane: Mix the polymer bottom membrane material CA, inorganic particle zinc hydroxide, and solvent N,N-dimethylformamide, stir at 70°C for 24h, until the membrane liquid is uniform, and then place in a vacuum The inorganic particles / polymer film liquid is obtained by degassing in an oven; the mass ratio of the polymer bottom film material, inorganic particles, and solvent is 100:70:1300; the obtained film liquid is coated with a scraping film on a polyester non-woven fabric, Using water as the gel bath, the membrane is prepared by the immersion precipitation phase inversion method, so that the solvent and water in the membrane liquid can be exchanged thoroughly;

[0034] 2) In situ preparation of MOFs membrane: dissolve the organic ligand 2-ethylimidazole and the metal salt zinc hydroxide in the solvent methanol respectively, add concentrated ammonia water and mix evenly, and immerse the bottom membrane prepared in step 1) into the orga...

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Abstract

The invention provides a method for preparing a pervaporation layer-by-layer assembly membrane for gasoline desulfurization. The layer-by-layer assembly membrane is a multilayer composite membrane containing more than three layers. The preparation method of the layer-by-layer assembly membrane includes step S1: preparing a porous Supporting the base film, step S2: in-situ growth of metal-organic framework membrane (MOFs film) on the base film, step S3: coating polyethylene glycol on the surface of MOFs film to form the composite film, that is, MOFs / PEG layer-by-layer assembly film ; and the metal element contained in the inorganic particles used in step S1 is the same as the metal element contained in the metal salt in step S2. The MOFs / PEG layer-by-layer assembly membrane prepared by the present invention has good sulfur-enrichment effect on sulfur-containing gasoline, high sulfur-enrichment factor, and good permeation flux. The sulfur-enrichment factor of the MOFs / PEG layer-by-layer assembly membrane reaches up to 19.5, and the permeation flux is 3.583kg / m 2 h, has a good industrial application prospect.

Description

technical field [0001] The invention belongs to the field of pervaporation membrane separation, in particular to a method for preparing a pervaporation layer-by-layer assembly membrane for gasoline desulfurization. Background technique [0002] The sulfur compounds in gasoline will cause serious air pollution. The sulfur compounds in gasoline will generate sulfur oxides after combustion, which will form acid rain and pollute the environment when discharged into the air. Many countries in the world today limit the sulfur content in gasoline to within 10ppm ; Therefore, in the face of increasingly stringent environmental protection standards, the production of ultra-low sulfur gasoline has become a standard requirement in the oil refining industry, and the improvement of gasoline desulfurization technology is a major research topic we have to face. Gasoline is a petroleum refined product composed of alkanes, a mixture of C5-C14 olefins and naphthenes, and aromatic compounds. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D61/36B01D67/00B01D71/06B01D71/38C10G31/11
CPCB01D61/362B01D67/0006B01D71/06B01D71/38C10G31/11
Inventor 展侠王梦妍葛蕊王诗宇周子安
Owner BEIJING TECHNOLOGY AND BUSINESS UNIVERSITY
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