IP Library Granted Patent US 10,301,206
Granted Patent B2
US 10,301,206 · App. 15/717,497 · Granted May 28, 2019

Chemical free and energy efficient desalination system

Inventors: Amnon Levy (Ramat Hasaron, IL); Boris Liberman (Tel Aviv, IL); Gal Greenberg (Ein Sarid, IL)
Assignee: I.D.E. TECHNOLOGIES LTD
C02F9/00B01D61/022B01D61/025B01D61/04B01D61/06B01D61/08B01D65/02B01D65/08C02F1/32C02F1/441C02F1/461C02F3/301B01D2311/04B01D2311/06B01D2311/08B01D2321/04B01D2321/12B01D2321/2033C02F1/001C02F1/24C02F1/445C02F1/4674C02F1/78C02F3/06C02F3/104C02F3/223C02F3/34C02F2101/12C02F2101/30C02F2103/08C02F2201/009
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 10,301,206
App. No.
15/717,497
Granted
May 28, 2019
Kind
B2
Abstract

A desalination system ( 100 ) having an intake unit ( 110 ) providing seawater to a pre-treatment unit ( 120 ) connected to a reverse osmosis (RO) desalination unit ( 130 ) and a post treatment unit ( 150 ). The desalination system ( 100 ) is configured to operate without any external addition of chemicals to simplify logistics and regulation concerns. The units of the system are configured to prevent biofouling, scaling and corrosion by mechanical and biological means including high flow speeds, biological flocculation of colloids, and making the water entering the RO units inhospitable to bacteria and other organisms that cause biofouling, hence preventing their settlement and removing them with the brine. Recovery rate is lowered and energy is recovered to increase the energetic efficiency and minerals that are added to the product water are taken from the brine.

Claims (21)

1. A method of operating a reverse osmosis desalination system, the method comprising:

supplying seawater at a flowing speed between 1.5 and 3 m/sec selected to prevent larvae settling in an intake pipeline,

biologically flocculating organic and mineral colloids in the supplied seawater to generate floc,

mechanically removing the floc to generate an accessible organic carbon level lower than 2.5 ppm,

reducing an oxygen content below saturation to prevent microbial attachment to membranes and growth in the water, to produce feed water,

extracting product water and brine from the feed water by reverse osmosis, and

disinfecting the product water.

2. The method of claim 1 , further comprising daily back washing a reverse osmosis membrane to remove bacteria from the biological flocculation therefrom.

3. The method of claim 1 , further comprising providing the seawater to the biological flocculating at a flowing speed between 15 and 60 m/hour.

4. The method of claim 1 , further comprising not adding any acids, pH regulators, ferric compounds, antiscalants, chlorine, coagulants and flocculants, or biocides.

5. A method of operating a reverse osmosis desalination system, the method comprising:

supplying seawater in an intake pipeline at a flowing speed between 1.5 and 3 m/sec selected to prevent larvae settling in the intake pipeline,

biologically flocculating organic and mineral colloids in the seawater supplied from the intake pipeline to generate floc,

mechanically removing the floc to generate an accessible organic carbon level lower than 2.5 ppm,

reducing an oxygen content below saturation to prevent microbial attachment to membranes and growth in the water, to produce feed water,

extracting product water and brine from the feed water by reverse osmosis,

disinfecting the product water, and

simultaneously recovering gauge and osmotic power from the brine and operating the reverse osmosis at a recovery rate reduced from a maximal recovery rate by 10%.

6. The method of claim 5 , further comprising daily back washing a reverse osmosis membrane to remove bacteria from the biological flocculation therefrom.

7. The method of claim 5 , further comprising providing the seawater supplied from the intake pipeline for the biological flocculation at a flowing speed between 15 and 60 m/hour.

8. The method of claim 5 , further comprising not adding any acids, pH regulators, ferric compounds, antiscalants, chlorine, coagulants and flocculants, or biocides.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 9, 2021
From: IDE TECHNOLOGIES LTD.
To: IDE WATER TECHNOLOGIES LTD.
Reel/Frame 058053/0949 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 27, 2017
From: LIBERMAN, BORIS; LEVY, AMNON; GREENBERG, GAL
To: I.D.E. TECHNOLOGIES LTD
Reel/Frame 043718/0068 →
Continuity (3)
Continuation 14823991 · Aug 11, 2015
Continuation 13982748
Related Publication 20180016173A1 · Jan 18, 2018
Cited By (1)
US 12,209,034