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Membrane fouling and cleaning method of brine refining process by membrane method

A brine refining and membrane fouling technology, which is applied in the field of membrane fouling cleaning, can solve problems affecting the application and promotion of membrane brine refining technology, poor barium sulfate pollution removal effect, and patent publication of cleaning methods, etc., to achieve rapid membrane flux loss, The effect of restoring membrane flux loss and removing membrane fouling

Active Publication Date: 2010-07-14
NANJING UNIV OF TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Backflushing can restore part of the membrane flux, but due to the adsorption and deposition of some precipitated particles on the membrane surface and in the membrane pores, the pollution cannot be removed by backflushing, and must be removed by acid washing to dissolve the precipitated particles
Pickling has a good removal effect on calcium carbonate and magnesium hydroxide pollution, but because barium sulfate particles are insoluble in acid, the membrane flux cannot be restored due to the continuous accumulation of barium sulfate pollution during long-term operation and cleaning.
Ordinary acid, alkali, and oxidant cleaning methods are extremely ineffective in removing barium sulfate contamination. Replacing membrane elements due to the inability to restore membrane flux will undoubtedly greatly increase costs and affect the application and promotion of membrane brine purification processes.
[0004] At present, there is no membrane cleaning agent suitable for membrane brine refining on the market, and there is no patent publication on the cleaning method of membrane pollution in membrane brine refining. However, the promotion and application of membrane technology in the chlor-alkali industry and the salt industry urgently needs to be developed. A membrane pollution cleaning method suitable for membrane brine purification with easy-to-obtain raw materials, simple operation and outstanding effect

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] The composition and content of a kind of membrane cleaning agent are as follows:

[0021] A. Diethylenetriaminepentaacetic acid (DTPA) 750g

[0022] B. Oxalic acid 250g

[0023] C. Sodium hydroxide makes the cleaning agent pH=14

[0024] D. Water 20L

[0025] To clean the ceramic membrane, first use compressed gas to push the permeate to recoil, the recoil pressure is 0.2MPa, and the recoil time is 15s; then pickling, the mass concentration of hydrochloric acid is 2.5%, and the pickling temperature is 15°C. The membrane surface flow velocity is 0.5m / s, the transmembrane pressure is 0.01MPa, and the pickling time is 90min; the membrane cleaning agent is used for cross-flow filtration cleaning, the transmembrane pressure difference is 0.05MPa, and the membrane surface flow velocity is 0.5m / s. The cleaning temperature is 15°C, and the cleaning time is 360 minutes. After cleaning, the pure water flux of the membrane returns to 99.8% of the pure water flux of the new memb...

Embodiment 2

[0027] The cleaning agent formula and the ceramic membrane used are the same as in Example 1. Firstly, recoil is carried out, the recoil pressure is 0.7 MPa, and the recoil time is 3s; then pickling is carried out, the mass concentration of hydrochloric acid is 15%, and the pickling temperature is 40°C. The membrane surface flow velocity is 4m / s, the transmembrane pressure is 0.3MPa, and the pickling time is 20min; the membrane cleaning agent is used for cross-flow filtration cleaning, the transmembrane pressure difference is 0.3MPa, the membrane surface flow velocity is 4m / s, and the cleaning temperature The temperature is 75°C, and the cleaning time is 20 minutes. After cleaning, the pure water flux of the membrane returns to 99.9% of the pure water flux of the new membrane.

Embodiment 3

[0029] The composition and content of a kind of membrane cleaning agent are as follows:

[0030] A. Ethylenediaminetetraacetic acid (EDTA) 4g

[0031] B. Citric acid 2g

[0032] C. Potassium hydroxide makes the cleaning agent pH=13

[0033] D. Water 20L

[0034] To clean the ceramic membrane, first perform recoil, the recoil pressure is 0.4MPa, and the recoil time is 10s; then pickling, the mass concentration of sulfuric acid is 5%, the pickling temperature is 45°C, and the membrane surface flow rate is 0.5m / s, the transmembrane pressure is 0.1MPa, and the pickling time is 60min; the membrane cleaning agent is used for dead-end filter cleaning, the transmembrane pressure difference is 0.02MPa, the cleaning temperature is 20°C, and the cleaning time is 400min. The pure water flux of the membrane was restored to 99.4% of the pure water flux of the new membrane.

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PUM

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Abstract

The invention discloses a membrane fouling and cleaning method, in particular to a membrane fouling and cleaning method of brine refining process by the membrane method, which is suitable for chlor-alkali industry and salt making industry, and comprises the following specific steps: firstly, carrying out back flushing for clearing filter cakes deposited on the surface of the membrane; secondly, carrying out acid cleaning for clearing calcium carbonate and magnesium hydroxide particle fouling remained after the back flushing; and finally, cleaning by using a membrane cleaning agent for clearing barium sulfate particle fouling which can not be cleared by the acid cleaning. The membrane fouling and cleaning method provided by the invention has the following beneficial effects of easily obtained raw materials and convenient use, can effectively clear membrane fouling, reduce membrane cleaning frequency, improve the stability of a membrane system, reduce energy consumption, can completely and rapidly restore membrane flux loss, speed up the regeneration of the membrane system, has no damage to the membrane and ensures the consistency of membrane properties before and after cleaning.

Description

technical field [0001] The invention relates to a membrane fouling cleaning method, in particular to a membrane fouling cleaning method suitable for the membrane brine refining process in the chlor-alkali industry and the salt making industry. Background technique [0002] Membrane fouling refers to the phenomenon that certain components in the feed liquid system deposit on the membrane surface or in the membrane pores during the membrane separation process, resulting in a continuous decrease in the membrane filtration flux. In the application process, the membrane must be cleaned and regenerated after the membrane fouling reaches a certain level, so as to restore the filtration flux and retention performance of the membrane. For seriously polluted membranes, it is usually cleaned alternately with strong acid and strong alkali, and oxidants such as sodium hypochlorite and surfactants are added. This method can remove most inorganic and organic pollutants and biological pollu...

Claims

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Application Information

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IPC IPC(8): B01D65/02
Inventor 邢卫红顾俊杰仲兆祥刘飞徐南平
Owner NANJING UNIV OF TECH
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