IP Library Granted Patent US 10,988,395
Granted Patent B2
US 10,988,395 · App. 16/581,561 · Granted Apr 27, 2021

Cerium-lanthanum treatment method for reduction of contaminants in wastewater membrane bioreactors

Inventors: Pamela Leigh Cornish (White Lake, MI); Mason Reames Haneline (Orange, CA)
Assignee: Neo Chemicals & Oxides, LLC
C02F3/1215B01D61/16B01D61/22C02F1/5236C02F1/5245C02F3/1268C02F3/1273B01D2311/04B01D2311/12B01D2311/246B01D2311/2642B01D2311/2688B01D2315/06C02F2101/105C02F2209/003C02F2209/08C02F2209/10C02F2209/11C02F2209/18C02F2209/22C02F2209/40Y02W10/10
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Quick Facts
Patent No.
US 10,988,395
App. No.
16/581,561
Granted
Apr 27, 2021
Kind
B2
Abstract

Disclosed are methods of treating wastewater using a membrane bioreactor and achieving a target phosphorus concentration for the membrane permeate stream. These methods include the steps of dosing a wastewater stream with a rare earth clarifying agent and passing the dosed wastewater stream through the membrane to obtain a membrane permeate stream with a permeate concentration that is less than the phosphorus concentration of the influent stream. This permeate concentration also can be equal to or less than a target phosphorus concentration. In the methods as disclosed herein, the rare earth clarifying agent can be chloride salts of one or more rare earth elements and in certain embodiments, the rare earth clarifying agent can be CeCl 3 and LaCl 3 .

Claims (30)

1. A method for treating wastewater using a membrane bioreactor comprising:

dosing a wastewater stream, as part of a membrane bioreactor system, containing a first concentration of phosphorus with a dose amount of a rare earth clarifying agent to obtain a dosed wastewater stream, the first concentration of phosphorus being greater than a target concentration of phosphorus; and

passing the dosed wastewater stream through a membrane of the membrane bioreactor system to obtain a membrane permeate stream, the membrane permeate stream having a permeate concentration of phosphorus less than the first concentration phosphorus.

2. The method of claim 1 , wherein the rare earth clarifying agent comprises chloride salts of a mixture of rare earth elements.

3. The method of claim 2 , wherein the rare earth clarifying agent comprises CeCl 3 and LaCl 3 .

4. The method of claim 3 , wherein the rare earth clarifying agent comprises from 55.0-75.0% by weight CeCl 3 , from 25.0-45.0% by weight LaCl 3 , and any balance being chloride salts of other rare earth elements.

5. The method of claim 4 , wherein the rare earth clarifying agent comprises from 55.0-75.0% by weight CeCl 3 , from 25.0-45.0% by weight LaCl 3 , and any balance of chloride salts of any one or more other rare earth elements being less than 1% by weight.

6. The method of claim 4 , wherein the rare earth clarifying agent comprises from 59.8-70.1% by weight of chloride salts of Ce, 29.9-40.1% by weight of chloride salts of La, and any balance of being chloride salts of any one or more other rare earth elements, wherein the balance is less than 1% by weight.

7. The method of claim 3 , wherein the rare earth clarifying agent comprises from 60.0-65.5% mol Ce and 30.0-40.0% mol La based on the total moles of rare earth elements and any balance being one or more of chloride salts of other rare earth elements.

8. The method of claim 3 , wherein the rare earth clarifying agent comprises CeCl 3 and LaCl 3 and less than 2% chloride salts of other rare earth elements.

9. The method of claim 2 , wherein the rare earth clarifying agent comprises chloride salts of a mixture of light rare earth elements.

10. The method of claim 1 , wherein the membrane permeate stream has a permeate concentration of phosphorus equal to or less than the target concentration of phosphorus.

11. The method of claim 1 , further comprising:

adjusting the dose amount of the clarifying agent based on the permeate concentration of phosphorus.

12. The method of claim 1 , further comprising:

increasing the dose amount of the clarifying agent if the permeate concentration of phosphorus is greater than the target concentration of phosphorus so that the permeate concentration of phosphorus is equal to or less than the target concentration of phosphorus.

13. The method of claim 1 , further comprising:

holding the dosed wastewater stream for a residence time before passing the dosed wastewater stream through the membrane.

14. The method of claim 1 , wherein the dose amount of the clarifying agent is from about 0.0005 to about 5.0 mmol RE/L wastewater.

15. The method of claim 1 , wherein the dose amount of the clarifying agent is from about 0.005 to about 1.0 mmol RE/L wastewater.

16. The method of claim 1 , wherein the dose amount of the clarifying agent is from about 0.01 to about 0.2 mmol RE/L wastewater.

17. The method of claim 1 , wherein the membrane bioreactor system is operated without fouling of the membrane from 25 to 75% longer than operation of a membrane bioreactor using a ferric clarifying agent.

18. The method of claim 17 , wherein the membrane bioreactor system is operated without fouling of the membrane from 35 to 70% longer than operation of a membrane bioreactor using a ferric clarifying agent.

19. The method of claim 17 , wherein the membrane bioreactor system is operated without fouling of the membrane from 45 to 65% longer than operation of a membrane bioreactor using a ferric clarifying agent.

20. The method of claim 1 , wherein the target concentration of phosphorus is a limit of 0.05 mg/L to 1.0 mg/L.

21. The method of claim 1 , wherein the rare earth clarifying agent comprises chloride salts of a pure rare earth element.

22. A method for treating wastewater using a membrane bioreactor comprising:

dosing a wastewater stream, as part of a membrane bioreactor system, containing a first concentration of phosphorus with a dose amount of a rare earth clarifying agent comprising CeCl 3 and LaCl 3 to obtain a dosed wastewater stream, the first concentration of phosphorus being greater than a target concentration of phosphorus;

removing at least some of the phosphorus as precipitated sludge from the wastewater stream; and

passing the dosed wastewater stream through a membrane of the membrane bioreactor system to obtain a membrane permeate stream, the membrane permeate stream having a permeate concentration of phosphorus less than the first concentration phosphorus.

Assignments (6)
CORRECTIVE ASSIGNMENT TO CORRECT THE 1ST RECEIVING PARTY NAME PREVIOUSLY RECORDED AT REEL: 72448 FRAME: 18. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT . Recorded Apr 30, 2026
From: NEO WATER TREATMENT LLC
To: NEO WATER TREATMENT, LLC; MP MINE OPERATIONS LLC
Reel/Frame 075494/0637 →
SHORT FORM PATENT SECURITY AGREEMENT Recorded Sep 5, 2025
From: MP MINE OPERATIONS LLC; SECURE NATURAL RESOURCES LLC
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 072818/0718 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 29, 2025
From: NEO WATER TREATMENT LLC
To: MP MINE OPERATIONS LLC
Reel/Frame 072448/0018 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 2, 2021
From: NEO CHEMICALS & OXIDES, LLC
To: NEO WATER TREATMENT LLC
Reel/Frame 056744/0621 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 21, 2021
From: NEO CHEMICALS & OXIDES, LLC
To: NEO WATER TREATMENT LLC
Reel/Frame 056608/0790 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 28, 2021
From: CORNISH, PAMELA LEIGH; HANELINE, MASON REAMES
To: NEO CHEMICALS & OXIDES, LLC
Reel/Frame 055746/0435 →
Continuity (2)
Provisional Application 62736122 · Sep 25, 2018
Related Publication 20200095144A1 · Mar 26, 2020