Split flow EDI apparatus for treating second pass RO permeate water with high flow rate
We report an electro-deionization (EDI) device having split flow arrangement for the purification of second pass RO permeate water with high flow rate in which the feed water is fed through the center port and is diverted into each section of dilute chamber with equal flow rate, producing two product streams. The EDI device has concentrate chambers adjacent to dilute chambers in two sections of the stack, allowing independent flow through the separate sections. The split flow design reduces resin bed depth requirement for processing of second pass RO permeate water. This results in higher flow rate through the stack, elimination of the pressure drop limitation, and reduction of power consumption per unit volume of water.
1. An electrodeionization apparatus comprising:
a first end plate;
a first electrode house plate (“EHP”) located adjacent to the first end plate, said EHP comprising two cathodes, cationic resin, and an anion membrane;
a plurality of cell pairs comprising alternating concentrate chambers and dilute chambers, wherein each concentrate chamber comprises a concentrate spacer placed over an anion membrane,
wherein each concentrate chamber comprises two independent concentrate sections separated by a concentrate rib, said concentrate sections comprising a conductive mesh, wherein each of said concentrate sections has separate concentrate inlet ports and concentrate outlet ports; and
wherein each dilute chamber comprises a cation membrane oriented toward the first EHP, a dilute spacer, and an anion membrane, wherein each dilute chamber comprises two independent dilute sections separated by a dilute rib and fed by a common feed port that splits flow of feed water equally into the independent dilute sections, each of said dilute sections having separate product ports;
a second end plate; and
a second EHP located adjacent to the second end plate, said second EHP comprising two anodes, a cationic membrane, and cation resin media.
2. The electrodeionization apparatus of claim 1 , further comprising a product header for collecting and combining product water from each of said product ports.
3. The electrodeionization apparatus of claim 1 , comprising 30-35 cell pairs.
4. The electrodeionization apparatus of claim 1 , comprising at least 30 cell pairs.
5. The electrodeionization apparatus of claim 1 , further comprising a plurality of EPDM rings between the concentrate spacers and dilute spacers.
6. An combined electrodeionization apparatus comprising a plurality of electrodeionization apparatus of claim 1 connected in series.
7. The electrodeionization apparatus of claim 1 , wherein the electrodeionization capacity of the apparatus is twice that of an electrodeionization apparatus having the same number of cells and same membrane area but single-section dilute spacers and single-section concentrate spacers.