Anaerobic treatment of industrial wastewater
Feed water is processed in an anaerobic digester. A solid-liquid separation device, for example a sludge screw thickener, treats a stream drawn from the digester in a recirculation loop. The solids portion is returned to the digester to increase the solids retention time and the TSS concentration in the digester. A liquid portion with less than 5% of the solids in the stream is removed and optionally treated further. The flow rate to the solid-liquid separation device is preferably greater than the influent flow rate. The solid-liquid separation device may receive digestate at a TSS concentration of 4% or more and return a solids portion having a TSS concentration of over 10%. The feed water is preferably one or more industrial waste streams having a COD concentration of 20,000 to 50,000 mg/L and a TSS concentration from 1-5%. The organic loading rate may be 10-12 kg/COD/m3/day.
1. A method for treating wastewater comprising steps of,
a) feeding an influent having a total suspended solids concentration of about 1-5% at a flow rate Q to an anaerobic digester;
b) feeding a mixture from the anaerobic digester a flow rate of Q or more to a solid liquid separation device;
c) separating the mixture into a liquid portion and a solids portion; and,
d) returning at least most of the solids portion to the anaerobic digester.
2. The method of claim 1 wherein the solid liquid separation device is a screw thickener.
3. The method of claim 1 wherein substantially all of the solids portion is returned to the anaerobic digester.
4. The method of claim 1 wherein the anaerobic digester has a TSS concentration of 4 to 7%.
5. The method of claim 1 wherein the solids portion has a TSS concentration of over 10%.
6. The method of claim 1 wherein the solids portion has a TSS concentration of over 12%.
7. The method of claim 1 wherein the solids portion has a TSS concentration in the range of 12-14%.
8. The method of claim 1 wherein the organic loading rate of the anaerobic digester is at least 10 kg/COD/m3/day.
9. The method of claim 1 wherein the influent has a chemical oxygen demand concentration of about 20,000 to 50,000 mg/L.
10. The method of claim 1 wherein the solids portion contains 95% or more of the suspended solids in the mixture.
11. The method of claim 1 wherein the solids portion has a TSS concentration that is at least twice the TSS concentration of the mixture.
12. The method of claim 1 further comprising a step of treating the liquid portion in a second solid liquid separation device.
13. The method of claim 12 wherein the second solid liquid separation device is selected from the group consisting of a dissolved air flotation unit, a cavitation air flotation unit, and a tubular membrane.
14. The method of claim 12 wherein the second solid liquid separation device is a dissolved air flotation unit.
15. The method of claim 1 further comprising a step of treating the liquid portion in an activated sludge reactor.
16. The method of claim 15 wherein the activated sludge reactor is a membrane bioreactor.
17. The method of claim 1 further comprising a step of treating the liquid portion in an anaerobic membrane bioreactor.
18. The method of claim 1 further comprising a step of adding a polymer to the mixture.