Biofilm carrier media in moving bed biofilm reactor processes

Patent metadata

Field	Value
Publication number	US-12110243-B2
Application number	US-201916964985-A
Country	US
Kind code	B2
Filing date	Jan 29, 2019
Priority date	Jan 29, 2018
Publication date	Oct 8, 2024
Grant date	Oct 8, 2024

Abstract

The invention pertains to a bio-carrier to carry a biofilm in a moving bed biofilm reactor (MBBR), the carrier being a particle comprising dehydrated sludge. The use of a bio-carrier in a MBBR process to purify a liquid from contaminants is disclosed and a method of manufacture of a bio-carrier is provided.

First claim

The invention claimed is:

1. A bio-carrier for carrying a biofilm in a moving bed biofilm reactor (MBBR) comprising:
the bio-carrier comprising a dehydrated sludge particle; wherein the bio-carrier is a virgin carrier and a mobile structure configured to support and carry a biofilm in a MBBR;
wherein the dehydrated sludge particle has a nominal diameter of 0.7 to 7 mm, the dehydrated sludge particle has a volumetric mass density of 1.02 to 1.8 g/cm 3 , as determined by weighing the dehydrated sludge particle in air and then in ethanol (99.9 vol-%) at 20 0C and 1 atm, and the dehydrated sludge particle has a water content between 0 and 50 weight-%, as measured as water content fraction of the dehydrated sludge particle on total mass basis;
wherein the particle has a settling velocity in the range of 0.02 m/s to 0.4 m/s in denatured ethanol (99.9 vol.- % ethanol) at 20 0C and 1 atm.

2. A bio-carrier according to claim 1 , wherein the dehydrated sludge particle is comprised of sludge from a water purification process and/or or an organic solids treatment process.

3. A bio-carrier according to claim 2 , wherein the sludge is primary, secondary or tertiary sludge from a municipal or industrial wastewater treatment process or any combination thereof or digested sludge from an organic solids treatment process.

4. A bio-carrier according to claim 3 , wherein the sludge have been digested in an anaerobic digester.

5. The bio-carrier according to claim 1 , wherein the particle has a weight of 0.1 to 100 mg.

6. The bio-carrier according to claim 1 , wherein the particle has a nominal diameter of 0.9 to 4 mm.

7. The bio-carrier according to claim 1 , wherein the particle has an inorganic content between 0 and 90 weight-%, as measured as ash content fraction of the particle on dry mass basis.

8. A method of biologically treating water or wastewater containing contaminants:
directing the water or wastewater into a MBBR;
placing a plurality of the bio-carriers of claim 1 into the MBBR;
continuously or intermittently aerating or mixing the water or wastewater in the MBBR so as to maintain dehydrated sludge particles of the bio-carriers in suspension;
wherein the dehydrated sludge particles of the bio-carriers provide surfaces for biofilm growth; growing biofilms on the dehydrated sludge particles of the bio-carriers in the MBBR; and
biologically treating the water or wastewater in the MBBR as the biofilms on the dehydrated sludge particles biodegrade the contaminants in the water or wastewater.

9. The method according to claim 8 wherein the MBBR comprises one or more connected volumes or zones in which biological activity is promoted, one or several inlets for providing water or wastewater to be treated, one or several outlets for withdrawing treated water or wastewater, and one or more aerators or mixers.

10. The method according to claim 8 , wherein the aerating is intermittent aeration; or the mixing is intermittent mixing.

11. The method according to claim 8 further including: intermittently withdrawing treated water or wastewater from the MBBR; and retaining the dehydrated sludge particles of the bio-carriers and the biofilm thereon in the MBBR as the treated water or wastewater is withdrawn by deactivating the aerating or mixing in the MBBR, thereby allowing the dehydrated sludge particles of the bio-carriers and the biofilm thereon to settle in the MBBR.

12. The method according to claim 8 wherein the treated water or wastewater is continuously withdrawn from the MBBR and the MBBR further comprises a screen, sieve, filter, membrane or phase separator to retain the dehydrated sludge particles and the biofilm thereon in the MBBR.

13. The method according to claim 8 , wherein the MBBR system further comprises a screen, sieve, filter, membrane, or phase separator to retain the bio-carrier in the MBBR.

14. The method according to claim 8 , wherein additional dehydrated sludge particles are placed in the MBBR periodically, daily, weekly, monthly, or annually, to replenish lost or spent the dehydrated sludge particles and the additional dehydrated sludge particles.

15. A method of manufacturing the bio-carrier of claim 1 comprising: (i) obtaining sludge from a sludge source; (ii) dehydrating the sludge to a total dry solids content of more than 65 wt.- %; and (iii) forming the dehydrated sludge into dehydrated sludge particles.

16. The method according to claim 15 , wherein dehydrating the sludge in step (ii) utilizes one or more sludge dehydration technologies selected from the group consisting of: thin layer drying, belt drying, rotary drum drying, disc drying, vertical drying, solar drying, vacuum drying, fluidized bed drier, and any combination thereof.

17. The method according to claim 15 , wherein the dehydrated sludge particles are formed in step (iii) by milling, grinding, cutting, crushing, pelletization, granulation, extrusion or pressing.

18. The method according to claim 15 , wherein steps (ii) and (iii) take place simultaneously, using a technique for both drying and mechanically forming the dehydrated sludge into the dehydrated sludge particles.

19. The method according to claim 15 , further including characterizing the dehydrated sludge particles from step (iii) and, based on the characterization, selecting dehydrated sludge particles for use in carrying a biofilm in the MBBR.

20. The method according to claim 15 , wherein the sludge is dewatered in a dewatering step (a), before the dehydration step (ii), to reach a total solids content between 5-50 wt.- %.

21. The method according to claim 15 , The method according to wherein the dewatering in step (a) utilizes one or more different technologies selected from the group consisting of settling techniques, centrifugation techniques, hydrocyclone techniques, dissolved air flotation techniques, and filter pressing techniques.

22. The method according to claim 15 , wherein one or more additives are added and mixed with the sludge before the dehydration step (ii), the one or more additives being an organic or inorganic components, affecting the volumetric mass density of the dehydrated sludge, a fibrous component increasing the mechanical strength of the dehydrated sludge particle, or a nutrient or mineral promoting biomass growth.

23. The bio-carrier according to claim 3 , wherein the sludge has been digested in an aerobic digester.

24. The method according to claim 19 wherein the dehydrated sludge particles are sorted by a technology selected from the group consisting of sieving, screening, air classification, and specific gravity separation, or any combination thereof.

25. The bio-carrier according to claim 1 wherein the dehydrated sludge particle includes an outer surface that includes compartments formed in the outer surface and configured to facilitate biofilm attachment to the dehydrated sludge particle.

26. A bio-carrier for receiving and supporting a biofilm in a moving bed bioreactor (MBBR), comprising:
the bio-carrier comprising a dehydrated sludge particle;
wherein the bio-carrier is a virgin carrier and a mobile structure;
the dehydrated sludge particle having an outer surface configured to attach to and grow a biofilm in a MBBR;
the dehydrated sludge particle having a nominal diameter of 0.7 to 7 mm;
the dehydrated sludge particle having a volumetric mass density of 1.02 to 1.8 g/cm 3 , as determined by weighing the particle in ai

Assignees

• Veolia Water Solutions & Tech

Inventors

• Magnusson Per
• Rosen Christian

Classifications

• C02F11/147

  using organic substances (C02F11/148 takes precedence) · CPC title

• C02F11/143

  using inorganic substances (C02F11/148 takes precedence) · CPC title

• C02F11/14

  with addition of chemical agents · CPC title

• C02F11/122

  using filter presses (C02F11/123 takes precedence) · CPC title

• C02F11/12

  by de-watering, drying or thickening · CPC title