Systems and methods for treating dilute wastewater
US-10464833-B2 · Nov 5, 2019 · US
US9783442B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9783442-B2 |
| Application number | US-201514866735-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 25, 2015 |
| Priority date | Sep 26, 2014 |
| Publication date | Oct 10, 2017 |
| Grant date | Oct 10, 2017 |
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Phagotrophic algae are used in connection with aerobic or anaerobic digestion of solids, especially waste activated sludge (WAS), to more efficiently digest solids and to meet, over a shorter period of time, volatile solids standards and specific oxygen uptake rate requirements as well as pathogen reduction requirements.
Opening claim text (preview).
We claim: 1. A method for effecting efficient digestion of waste activated sludge (WAS) in a wastewater treatment plant, comprising: introducing phagotrophic algae to WAS, to produce a WAS-algae mixture, subjecting the WAS-algae mixture to digestive conditions in a digestion process, maintaining the WAS-algae mixture in the digestion process for a period of time sufficient that concentration of WAS-consuming microorganisms in the mixture is rapidly reduced due to consumption by the phagotrophic algae and the algae become starved and rely on endogenous respiration resulting in degradation of the algae, and sufficient that preselected VS, SOUR and pathogen targets have been met in the digested mixture, to produce a digested biomass, and removing the resulting digested biomass from the digestion process. 2. The method of claim 1 , wherein the WAS-algae mixture is subjected to aerobic digestion, in a continuous process wherein the algae is introduced to the WAS in a first digestion stage or zone in which retention time is sufficient to allow the algae to establish into a stable population by consuming microbes, while moving a portion of the WAS-algae mixture out of the first stage or zone and into one or more further digestion stages or zones wherein retention time is sufficient to meet said targets, and including bringing additional WAS into the first stage on a continuous basis while removing digestive biomass that has met said targets. 3. The method of claim 1 , wherein the WAS-algae mixture is subjected to aerobic digestion, in a continuous, staged digestion process wherein the algae is introduced to the WAS in a first digestion stage in which retention time is sufficient to allow the algae to establish into a stable population by consuming microbes, and at intervals, moving a portion of the WAS-algae mixture out of the first stage and to one or more further digestion stages wherein retention time is sufficient to meet said targets, and including bringing additional WAS into the first stage at each interval as said portion of the WAS-algae mixture is moved out of the first stage. 4. The method of claim 1 , wherein the digestion process of the WAS-algae mixture is conducted in a batch process. 5. The method of claim 1 , wherein the WAS-algae mixture is subjected to anaerobic digestion. 6. The method of claim 1 , wherein the WAS-algae mixture is subjected to aerobic digestion. 7. The method of claim 1 , wherein the WAS-algae mixture is subjected to anaerobic digestion and is retained in the digester tank until substantially all microbes and algae have died off. 8. The method of claim 1 , wherein the WAS-algae mixture is retained in the digester tank until substantially all microbes and algae have died off. 9. The method of claim 1 , wherein the WAS-algae mixture includes primary sludge from the treatment plant. 10. The method of claim 1 , wherein the WAS-algae mixture is subjected to anaerobic digestion, and wherein the WAS includes primary sludge from the treatment plant. 11. The method of claim 1 , wherein the WAS is subjected to pretreatment involving raising pH above 7.5 and aeration of the WAS to disassociate sludge flocs in order increase accessibility of algae in consuming microorganisms. 12. The method of claim 1 , wherein VS reduction of at least 35% and SOUR reduction to below 1.5 mg/g TS/Hr are achieved within ten days.
by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title
use of algae · CPC title
Cross-Sectional Technologies · mapped topic
Biological treatment · CPC title
Anaerobic treatment; Production of methane by such processes · CPC title
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