IP Library Granted Patent US 12,404,193
Granted Patent B2
US 12,404,193 · App. 17/599,682 · Granted Sep 2, 2025

Flow through aerobic granular sludge system and method

Inventor: John Fraser (Arvada, CO)
Assignee: Carollo Engineers, Inc.
C02F3/301C02F1/006C02F3/1226C02F2203/004C02F2301/046
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12,404,193
App. No.
17/599,682
Granted
Sep 2, 2025
Kind
B2
Abstract

A flow through aerobic granular sludge (AGS) system includes a flow through reactor. The flow through reactor includes a first adsorption zone and first and second unaerated and aerated zones and may include a wastewater distribution system and a selector zone. The first adsorption zone includes AGS granules and may include a mixing device. The first and second unaerated zones are under anaerobic, anoxic, or both anaerobic and anoxic conditions and each may include a mixing device. The first and second aerated zones are under aerobic conditions and each may include an aeration device. The flow through reactor is configured such that the wastewater and AGS granules in the first adsorption zone flow continuously from the first adsorption zone through the first unaerated zone, the first aerated zone, the second unaerated zone, the second aerated zone, and optionally to the selector zone and out of the flow through reactor.

Claims (7)

1. A flow through aerobic granular sludge (AGS) system for treating wastewater comprising: a multi-pass flow through reactor comprising a first pass, a second pass downstream of the first pass, and a third pass downstream of the second pass, wherein each of the first pass, the second pass, and the third pass comprises an adsorption zone, an unaerated zone downstream of the adsorption zone, and an aerated zone downstream of the unaerated zone, and wherein at least the adsorption zone of the first pass includes AGS granules; a selector zone located downstream of the third pass, the selector zone configured to remove the AGS granules from the wastewater; and a return AGS pumping system in communication with the selector zone, the return AGS pumping system configured to transport the AGS granules removed from the wastewater in the selector zone to the adsorption zone of at least one of the following: the first pass, the second pass, the third pass, or any combination thereof, wherein the multi-pass flow through reactor is configured such that, at all stages of operation, the wastewater and AGS granules flow continuously and sequentially from the first pass to the second pass and from the second pass to the third pass.

2. The flow through aerobic granular sludge (AGS) system for treating wastewater of claim 1 , wherein the multi-pass flow through reactor further comprises:

a wastewater distribution system configured to introduce wastewater to at least the adsorption zone of the first pass.

3. The flow through aerobic granular sludge (AGS) system for treating wastewater of claim 2 , wherein the multi-pass flow through reactor further comprises:

a step feed channel configured to feed wastewater into the adsorption zone of each of the second pass and the third pass.

4. The flow through aerobic granular sludge (AGS) system for treating wastewater of claim 1 , wherein each of the first pass, the second pass, and the third pass comprises a plurality of unaerated zones and a plurality of aerated zones.

5. A method of treating wastewater using a multi-pass flow through aerobic granular sludge (AGS) reactor, wherein the multi-pass flow through AGS reactor comprises a first pass, a second pass downstream of the first pass, and a third pass downstream of the second pass, wherein each of the first pass, the second pass, and the third pass comprises an adsorption zone, an unaerated zone downstream of the adsorption zone, and an aerated zone downstream of the unaerated zone, and wherein at least the adsorption zone of the first pass includes AGS granules, the method comprising: introducing wastewater to the adsorption zone of the first pass; causing the wastewater and the AGS granules to continuously and sequentially flow at all stages of operation of the multi-pass flow through AGS reactor from the first pass to the second pass and from the second pass to the third pass; distributing the wastewater and at least a portion of the AGS granules to a selector zone located downstream of the third pass; and returning the AGS granules removed from the wastewater to the adsorption zone of at least one of the following: the first pass, the second pass, the third pass, or any combination thereof.

Assignments (2)
SECURITY INTEREST Recorded Jan 2, 2026
From: CAROLLO ENGINEERS, INC.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 073354/0226 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 29, 2021
From: FRASER, JOHN
To: CAROLLO ENGINEERS, INC.
Reel/Frame 057652/0084 →
Continuity (2)
Provisional Application 62827322 · Apr 1, 2019
Related Publication 20220194832A1 · Jun 23, 2022
References Cited (27)
US 4663044A · Goronszy · 1987 [cited by applicant]
US 5480548A · Daigger et al. · 1996 [cited by applicant]
US 7195712B2 · Park et al. · 2007 [cited by applicant]
US 7273553B2 · Van Loosdrecht et al. · 2007 [cited by applicant]
US 8017014B2 · Yoon et al. · 2011 [cited by applicant]
US 8747671B2 · Giraldo et al. · 2014 [cited by applicant]
US 9242882B2 · Nyhuis et al. · 2016 [cited by applicant]
US 10099951B2 · Reilly et al. · 2018 [cited by applicant]
US 10112856B2 · Bott et al. · 2018 [cited by applicant]
US 10590018B2 · Miyake et al. · 2020 [cited by applicant]
US 20070158265A1 · Cote et al. · 2007 [cited by applicant]
US 20100264080A1 · Livingston et al. · 2010 [cited by applicant]
US 20130075327A1 · Yuan et al. · 2013 [cited by applicant]
US 20150376043A1 · Wett et al. · 2015 [cited by applicant]
US 20160137537A1 · Bott · 2016 [cited by examiner]
US 20170203984A1 · Lee et al. · 2017 [cited by applicant]
US 20180339925A1 · Miyake et al. · 2018 [cited by applicant]
US 20200002201A1 · Stinson et al. · 2020 [cited by applicant]
US 20210070642A1 · Fraser · 2021 [cited by applicant]
CA 3074480A1 · 2019 [cited by applicant]
CN 105621615A · 2016 [cited by applicant]
EP 3279154A1 · 2018 [cited by applicant]
WO 2019046416A1 · 2019 [cited by applicant]
WO 2020104944A1 · 2020 [cited by applicant]
WO 2020205834A1 · 2020 [cited by applicant]
Katarzyna Chojnacka, Biosorption_and_bioaccumulation_-_NPL_-_2010.pdf (Year: 2010). [cited by examiner]
Peng Yongzhen, Inverted A2/O step feed coupled aerobic particle sludge reinforced synchronous nitrification/denitrification dephosphorization device, 2016 (Year: 2016). [cited by examiner]