High-permeability selective acid-resistant nanofiltration membrane material as well as preparation method and application thereof

A selective, nanofiltration membrane technology, applied in semi-permeable membrane separation, chemical instruments and methods, membranes, etc., can solve the problems of polluted environment, high energy consumption, low permeation selectivity, etc. simple effect

Active Publication Date: 2021-09-03
SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the phosphorus content in the sludge leachate is very high, if not effectively recycled, it will lead to the loss of phosphorus resources and pollute the environment
[0008] At present, nanofiltration technology uses commercial acid-resistant nanofiltration membranes for phosphoric acid purification and phosphorus resource recovery. They are interfacial polymeric membranes with low permeation selectivity, operating pressures above 50 bar, and phosphoric acid permeability coefficient <1.0LMHbar, so energy consumption is high. The operating cost is high. At the same time, because the performance of the nanofiltration membrane is not up to standard, many combined processes are added before and after, and the overall process chain is greatly extended.
Moreover, commercial films are mostly prepared by interfacial polymerization, which requires the participation of organic solvents, and the preparation process is not environmentally friendly.
Moreover, the composition of phosphoric acid-containing feed liquid is often very complex, especially waste liquid from phosphoric acid plant, sludge leachate, etc., which contain a variety of impurity ions. If nanofiltration is performed directly, serious fouling will occur, which will greatly reduce the service life of the membrane.

Method used

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  • High-permeability selective acid-resistant nanofiltration membrane material as well as preparation method and application thereof
  • High-permeability selective acid-resistant nanofiltration membrane material as well as preparation method and application thereof
  • High-permeability selective acid-resistant nanofiltration membrane material as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] A hollow fiber polysulfone base membrane was selected, MWCO=50k Da. First, the basement membrane was washed with deionized water for 1 h, and gas was purged for 1 min. The polycation electrolyte 5g / L PEI (MWCO=100k Da) dissolved in 1.5mol / L NaCl solution and the polyanion electrolyte 5g / L PSS (100k Da) dissolved in 1.5mol / L NaCl solution were alternately coated in the base film Hole, stay for 10 minutes; first coat PEI; after each layer is coated, wash with deionized water for 5 minutes, and gas purge for 1 minute; after coating 3 double layers, use 0.5wt. Rinse with water for 5 minutes and store in refrigerator or deionized water. Prepared membrane material test 500ppm magnesium chloride flux J and rejection rate R, J=17.2LMHbar, R=97.3%; filter 10% H 3 PO 4 +2g / L Al simulated phosphoric acid solution, test phosphoric acid flux Flux, Al rejection rate R Al and phosphoric acid permeability P p , Flux=3.42LMHbar, R Al =98.2%, P p = 94.1%. The prepared film was ch...

Embodiment 2

[0037] The same as the membrane-making method in Example 1, the polyanion electrolyte in Example 1 was replaced by a 5 g / L SPEEK (sulfonation degree of 70%) aqueous solution. Prepared membrane material test 500ppm magnesium chloride, J=15.2LMHbar, R=97.5%; filter 10% H 3 PO 4 +2g / L Al simulated phosphoric acid solution, Flux=3.05LMHbar, R Al =98.5%, P p = 91.7%.

Embodiment 3

[0039] The same as the membrane-making method in Example 1, the polyanion electrolyte in Example 1 was replaced by 5g / L PVS (200k Da) dissolved in 1.5mol / L NaCl solution. Prepared membrane material test 500ppm magnesium chloride, J=18.9LMHbar, R=96.7%; filter 10%H 3 PO 4 +2g / L Al simulated phosphoric acid solution, Flux=3.55LMHbar, R Al =97.1%, P p = 93.7%.

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Abstract

The invention discloses a high-permeability selective acid-resistant nanofiltration membrane material as well as a preparation method and application thereof. The nanofiltration membrane material comprises a dense separation layer which is formed by assembling an amine and a quaternary ammonium salt polycation electrolyte and a polyanion electrolyte material with sulfonic acid groups or sulfuric acid groups layer by layer; the concentration of the polycation is 0.1-20 g / L, and the polycation is dissolved in a salt solution of 0.05-5 mol / L; the used polyanion electrolyte polymer material is a polymer material with sulfonic acid groups or sulfuric acid groups, the concentration of polyanion is 0.1-20g / L, and the polyanion is dissolved in a 0.05-5mol / L salt solution; the dense separation layer of the nanofiltration membrane is formed by layer-by-layer assembly, and has better permeation selectivity and excellent acid-resistant stability than a commercial nanofiltration membrane. The retention rate of the membrane to multivalent cations is greater than 90%, the permeability of the membrane to phosphoric acid is greater than 80%, and the permeability of phosphoric acid is one order of magnitude layer than that of that of a commercial membrane. The high-permeability selective acid-resistant nanofiltration membrane material is used in phosphoric acid refining and recycling processes, inorganic compounds in phosphoric acid-containing feed liquid are removed through pretreatment, then substances such as large particles and colloids are removed through ultrafiltration, stable operation of a nanofiltration membrane process is achieved, high-purity phosphoric acid of different grades is obtained, and the high-permeability selective acid-resistant nanofiltration membrane material has wide application in the aspects of phosphoric acid refining and phosphoric acid recycling.

Description

technical field [0001] The invention relates to the field of refining and recovering phosphoric acid by membrane separation technology, in particular to a process for refining and recovering a phosphoric acid-containing material liquid by a highly permeable and selective acid-resistant nanofiltration membrane. Background technique [0002] Phosphate rock in nature is mainly used to produce phosphoric acid, and then phosphoric acid is used as raw material to further produce phosphate fertilizer and various phosphorus chemical products. Phosphoric acid production process is mainly divided into thermal phosphoric acid process and wet phosphoric acid process, among which the energy consumption and cost of wet process are lower than that of thermal phosphoric acid. The output of wet-process phosphoric acid in the world has accounted for 85%-90% of the total output of phosphoric acid. However, wet-process phosphoric acid products have low purity and contain various impurity ions ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D61/00B01D67/00B01D71/68C01B25/238C01B25/234C01B25/237
CPCB01D61/027B01D67/0002B01D71/68C01B25/238C01B25/237C01B25/234B01D2325/30
Inventor 何涛徐姗姗孙楠何荣荣王一丹董晨俊宋健峰
Owner SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI
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