Method for cleaning separation membrane
A washing method and separation membrane technology, applied in semi-permeable membrane separation, chemical instruments and methods, membrane technology, etc., can solve the problems of decreased activated sludge activity, low device operation efficiency, long stop filtration time, etc. The effect of shortening, suppressing drug costs, and reducing equipment costs
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2008-10-01
Smart Images
Figure 1 Figure 2
Abstract
Description
technical field
[0001] The present invention relates to a method for washing a separation membrane, and more specifically, to a method for washing a separation membrane used in a membrane bioreactor method or the like. Background technique
[0002] Membrane separation activated sludge method is a method in which the water in the biological treatment tank for activated sludge treatment is filtered by a separation membrane to produce treated water. Compared with the conventional method of using a sedimentation tank, the space can be reduced, so We attract attention mainly on urban sewage treatment plants.
[0003] The separation membrane used includes an immersion type separation membrane installed inside the biological treatment tank and a separation membrane installed outside the biological treatment tank disclosed in Patent Document 1 (JP-A-9-136021). As for the immersion type separation membrane, as shown in Patent Document 1, there is known a method in which floating sol...
Examples
Embodiment
[0028] Such as figure 1As shown, the water in the activated sludge treatment tank of sewage is led out and circulated to the outside, and cross-flow filtration is performed through an internal pressure ceramic membrane. The separation membrane used is a monolithic membrane (membrane micropore diameter 0.1 μm, membrane pore diameter 4 mm) manufactured by the applicant company. As a result of operating under the conditions of circulating water volume of 1.0m / s and membrane filtration flow rate of 2.4m / d, the membrane permeation pressure rises rapidly, and stable operation cannot be performed even if original backwashing is performed every 45 minutes. In addition, 0.11m / s air was supplied from the gas supply device to make the raw water side of the membrane a gas-liquid mixed phase flow, but it still could not operate stably. In contrast, under the conditions of circulating water volume of 1.0m / s, membrane filtration flow rate of 2.4m / d, and gas flow rate of 0.11m / s, pulse backw...