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
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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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