Method and device for inhibiting membrane scaling in brackish water desalination treatment
A technology for desalination of brackish water and membrane inhibition, applied in seawater treatment, water/sewage treatment, chemical instruments and methods, etc., can solve the problems of high frequency of replacement of reverse osmosis membranes, waste of scale inhibitor, and inability to remove adhesions. , to achieve the effect of inhibiting membrane fouling, improving service time and improving effect
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Embodiment 1
[0039] see figure 1 , the present invention provides a technical solution:
[0040] A method for inhibiting membrane scaling in brackish water desalination treatment, comprising the following steps:
[0041] S1. Pretreatment of brackish water: remove colloids, suspended impurities, and reduce turbidity in brackish water by coagulation filtration; select FeCl 3 As a coagulant, the dosage is 1.0-2.5mg / L; after being mixed by a mixer, it is then filtered through a mechanical filter, so that the pollution index of the effluent water quality is <5, and the turbidity is <1;
[0042] S2. Dosing to eliminate residual chlorine: pump 1.5-3.0 mg / L sodium bisulfite through a metering pump, so that residual chlorine in brackish water reacts with sodium bisulfite to form neutral salt; control the concentration of brackish water The pH value is in the range of 7.0-7.5, and the free chlorine is controlled <0.1mg / L;
[0043] S3. Security filtration: set a set of security filters with a filtra...
Embodiment 2
[0054] The difference from Embodiment 1 is that the pulse pump 9 in Embodiment 1 is replaced by a constant pressure pump whose output pressure is 1.10 times of the reverse osmosis pressure. At the same time, the filtration accuracy of the security filter 2 is set to 5 μm. Change the design of the pulse pump 9, and use the constant pressure pump to continuously output to form a stable water film, which is perpendicular to the pressure direction of the osmotic pressure. This method can be used when the concentration of the concentrated solution is relatively high.
Embodiment 3
[0056] The difference from Example 1 is that there is no need to inject the antiscalant and hydrochloric acid separately, and hydrochloric acid is directly added to the antiscalant, and after mixing, it is pumped into the spiral pipeline 408 by a pulse pump at the same time.
[0057] To sum up: the present invention changes the traditional method of directly mixing the scale inhibitor with the raw water. When in use, the scale inhibitor is injected into the spiral pipeline to directly reach the surface of the reverse osmosis membrane module to form a scale inhibitor. The structure of the agent layer improves the inhibitory effect of membrane scaling; and using the reversing solenoid valve, hydrochloric acid can be injected within a specified time to descale the scaled surface, and can further inhibit membrane scaling and improve the efficiency of reverse osmosis membranes. usage time. In the design of the present invention, a pulse pump is also used as the delivery pump of the...
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