The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Nov. 12, 2019

Filed:

Mar. 23, 2018
Applicant:

Lehigh University, Bethlehem, PA (US);

Inventors:

Arup K. SenGupta, Bethlehem, PA (US);

Hang Dong, Bethlehem, PA (US);

Michael German, Bethlehem, PA (US);

Chelsey Shepsko, Englishtown, NJ (US);

Assignee:

LEHIGH UNIVERSITY, Bethlehem, PA (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 1/42 (2006.01); B01J 41/12 (2017.01); B01J 39/07 (2017.01); B01J 47/127 (2017.01); C02F 101/16 (2006.01); C02F 101/10 (2006.01); C02F 101/12 (2006.01); C02F 101/14 (2006.01); C02F 101/20 (2006.01); C02F 103/06 (2006.01);
U.S. Cl.
CPC ...
C02F 1/42 (2013.01); B01J 39/07 (2017.01); B01J 41/12 (2013.01); B01J 47/127 (2017.01); C02F 2001/422 (2013.01); C02F 2001/425 (2013.01); C02F 2101/101 (2013.01); C02F 2101/103 (2013.01); C02F 2101/105 (2013.01); C02F 2101/12 (2013.01); C02F 2101/14 (2013.01); C02F 2101/163 (2013.01); C02F 2101/203 (2013.01); C02F 2101/206 (2013.01); C02F 2103/06 (2013.01); C02F 2301/08 (2013.01); C02F 2303/16 (2013.01); C02F 2305/08 (2013.01);
Abstract

A method for purifying waste water, and a dual chamber purification system, in which feed water may be passed first through a hybrid anion exchange unit, and subsequently through a weak acid cationic exchange unit. The hybrid anion exchanger may comprise a hybrid sorbent (HAIX-NanoZr) with dual functional sorption sites. The weak acid cationic exchanger may be a fiber having a shell-core physical configuration with relatively short intra-particle diffusion path length so that the ion exchange sites reside predominantly on the periphery. The system may be used to achieve partial desalination or TDS reduction and concurrent removal of target contaminants (e.g., phosphate, hardness). Further, the system may be regenerated using COas the sole regenerant for both the hybrid anion exchanger and the weak acid cationic exchanger, thus producing spent regenerant with no externally added chemicals.


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