Method for constructing dynamic-like membrane to control membrane fouling of mbr
US-2024067545-A1 · Feb 29, 2024 · US
US10160679B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10160679-B2 |
| Application number | US-201515126886-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 11, 2015 |
| Priority date | Mar 20, 2014 |
| Publication date | Dec 25, 2018 |
| Grant date | Dec 25, 2018 |
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Wastewater is treated though primary treatment of the water by way of a micro-sieve to produce a primary effluent and primary sludge. There is secondary treatment of the primary effluent by way of a membrane bioreactor (MBR) or an integrated fixed film activated sludge (IFAS) reactor to produce a secondary effluent and a waste activated sludge. The micro-sieve may have openings of 250 microns or less, for example about 150 microns. In a process, a gas transfer membrane is immersed in water. Pressurized air flows into the gas transfer membrane. An exhaust gas is withdrawn from the gas transfer membrane and used to produce bubbles from an aerator immersed in the water.
Opening claim text (preview).
We claim: 1. A process comprising the steps of, a) immersing a gas transfer membrane in water; b) flowing pressurized air into the gas transfer membrane; c) withdrawing an exhaust gas from the gas transfer membrane; and, d) producing bubbles comprising the exhaust gas from an aerator immersed in the water, wherein the exhaust gas has a pressure larger than the static head of water above the aerator. 2. The process of claim 1 wherein the exhaust gas is supplied to the aerator without increasing the pressure of the exhaust gas. 3. The process of claim 1 further comprising supporting a biofilm on the gas transfer membrane and transferring oxygen to the biofilm. 4. The process of claim 1 further comprising a step of providing a suspended biomass in the water. 5. The process of claim 1 , wherein the water is anoxic or aerobic. 6. The process of claim 1 , wherein in step d) the bubbles are produced for 0.5 to 20 seconds at least once every 200 seconds or for 0.5 to 3 seconds at least once every 20 seconds. 7. An apparatus comprising, a first header, a second header, a plurality of gas transfer membranes extending between the headers, a gas inlet to the first header, a gas outlet from the second header, and an aerator connected to the gas outlet and located between or below the gas transfer membranes. 8. The apparatus of claim 7 , wherein the aerator comprises a transducer configured to release bursts of bubbles.
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