WO2000023382A1 - Method and apparatus for preventing scaling in electrodeionization units - Google Patents

Method and apparatus for preventing scaling in electrodeionization units Download PDF

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Publication number
WO2000023382A1
WO2000023382A1 PCT/CA1999/000882 CA9900882W WO0023382A1 WO 2000023382 A1 WO2000023382 A1 WO 2000023382A1 CA 9900882 W CA9900882 W CA 9900882W WO 0023382 A1 WO0023382 A1 WO 0023382A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
compartment
compartments
concentrating
aqueous solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/CA1999/000882
Other languages
English (en)
French (fr)
Inventor
David Florian Tessier
Robert Glegg
John H. Barber
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
E Cell Corp
Original Assignee
E Cell Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by E Cell Corp filed Critical E Cell Corp
Priority to DE69912985T priority Critical patent/DE69912985T2/de
Priority to IL14248899A priority patent/IL142488A0/xx
Priority to BR9914586-3A priority patent/BR9914586A/pt
Priority to MXPA01003822A priority patent/MXPA01003822A/es
Priority to EP99945796A priority patent/EP1133449B1/en
Priority to AU58438/99A priority patent/AU5843899A/en
Priority to AT99945796T priority patent/ATE254581T1/de
Priority to CA2347473A priority patent/CA2347473C/en
Priority to JP2000577118A priority patent/JP4805455B2/ja
Publication of WO2000023382A1 publication Critical patent/WO2000023382A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4602—Treatment of water, waste water, or sewage by electrochemical methods for prevention or elimination of deposits
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44—Ion-selective electrodialysis
    • B01D61/46—Apparatus therefor
    • B01D61/48—Apparatus therefor having one or more compartments filled with ion-exchange material, e.g. electrodeionisation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44—Ion-selective electrodialysis
    • B01D61/52—Accessories; Auxiliary operation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
    • C02F1/4695—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis electrodeionisation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/4611—Fluid flow
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/46115—Electrolytic cell with membranes or diaphragms

Definitions

  • the present invention relates to a method and apparatus for inhibiting scaling in
  • pure water is used for many industrial purposes such as, in processes for
  • Electrodeionization apparatus have recently been used with more frequency to
  • Electrodeionization generally
  • electrodeionization module comprises alternating arrangements of cation permeable
  • membranes and anion permeable membranes defining compartments therebetween.
  • ion exchange resin beads In alternating compartments, there is provided ion exchange resin beads.
  • compartments are known as diluting compartments.
  • the compartments which generally correspond to the compartments of the compartments of the compartments.
  • Such regions include those on the surface of the concentrate-
  • the present invention provides a method for inhibiting
  • compartments positioned between the anode and cathode compartments which comprises passing feed water to be deionized through the diluting compartments, passing water or
  • the water or aqueous solution may be
  • discharge of the diluting compartments in the electrodeionization unit can supply water
  • Salt can be inj ected into the water or aqueous solution
  • the present invention provides an electrodeionization unit for
  • deionizing water having an anode compartment at one end of the unit, a cathode
  • each of said concentrating compartments furthermore, each of said concentrating compartments further
  • compartment is defined by an anion exchange membrane and the porous diaphragm or
  • ion-conducting membrane and the second compartment is defined by the cation exchange membrane and the porous diaphragm or ion-conducting membrane wherein liquid in the
  • first compartment is prevented from mixing with liquid in the second compartment and
  • the present invention provides a method for inhibiting
  • concentrating compartments further comprising a porous diaphragm or ion-conducting
  • compartment is defined by the cation exchange membrane and porous diaphragm or ion-
  • such method comprising passing feed water to be deionized through the diluting
  • ions in the feed water migrate to the water or aqueous solution in the concentrating compartments.
  • the water or aqueous solution Prior to introduction to the concentrating compartment, the water or
  • aqueous solution can be treated for removal of metallic cations by a suitable unit
  • passed through the concentrating compartment can be supplied from a bleed of purified
  • Salt can be inj ected into the water or aqueous solution being supplied to the concentrating
  • Figure 1 is a schematic flowsheet of a first embodiment of the present
  • Figure 2 is a schematic flowsheet of a second embodiment of the present
  • Figure 3 is a schematic flowsheet of a third embodiment of the present
  • Figure 4 is a schematic flowsheet of a fourth embodiment of the present
  • FIG. 5 is a detailed schematic drawing of an electrodeionization unit of any
  • Figure 6 is a schematic flowsheet of a fifth embodiment of the present
  • compartments 32 each defined by anion exchange membrane 30 on the anode side and
  • Electrolyte solution is supplied to anode
  • diluting compartments 32 are provided in diluting compartments 32. These may comprise either
  • Water to be treated is introduced into the diluting compartments 32 from supply
  • Stream 44 can also supply flowstreams 36
  • compartments 32 migrate through cation exchange resins using ion exchange
  • compartments 32 migrate through anion exchange resins using ion exchange
  • anion exchange membranes 30 which are in
  • Hydroxyl ions migrate through the anion exchange
  • compartment 32 and adsorbed on ion exchange material 40 is greater than for other
  • anion exchange membrane 30 Because the scale-forming metallic cations tend to exist
  • Such supply stream 44 is relatively free of scale-forming metallic cations, and therefore
  • stream 50 comprises of water purified by the electrodeionization unit 10, the dissolved
  • compartment 18 This can involve injecting a solution of an inert salt from storage vessel 45, such as sodium chloride or potassium chloride, into supply stream 44 by means of a
  • metering pump 47 As an example, metred injection of 100 g/L sodium chloride solution
  • electrodeionization unit 10 is operated in series with reverse osmosis unit 62 for the
  • Water to be treated is supplied into the reverse osmosis unit 62 by
  • the permeate stream 66 is
  • retentate stream 68 either is discharged to drain or is used for other purposes
  • a bleed is taken from the permeate stream 66 and connected
  • supply stream 44 contain sufficiently low scale-forming metallic cation
  • compartment 18 may be insubstantial.
  • metallic cations in supply stream 44 is less than 5 ppm as calcium carbonate, and more
  • supply stream 44 may contain low salt concentrations and, as a result, may not be
  • electrodeionization unit 10 Accordingly, to mitigate this problem, it may be desirable to inject saline solution into supply stream 44 to increase the conductivity of the water
  • the bleed from supply stream 64 can be subjected to upstream pre-treatment by
  • pre-treatment means include mechanical filtration, classification, or activated carbon adsorption. Water bled from supply stream 64 is supplied into
  • softening unit 80 by supply stream 82. Softening is usually accomplished by means of ion exchange.
  • softening unit 80 can comprise of a sodium-cycle softener
  • Similar ion exchange softeners may employ other regenerating chemicals, such as potassium chloride or mineral acids, or other types of ion exchange
  • resins such as weak acide cation exchange resin.
  • the discharge stream 84 from the softening unit 80 may be connected to the
  • Dissolved salt concentrations in discharge stream 84 are sufficiently high such that additional salt injection is typically
  • FIGS. 6 and 7 illustrate a further embodiment of the present invention wherein
  • an electrodeionization unit 100 has concentrating compartments 118 which are divided
  • first and second compartments 119a and 119b by a porous diaphragm or ion-
  • Porous diaphragm can be composed of
  • a suitable commercially available porous diaphragm is MFTM
  • Ion-conducting membranes can be any material that can be used to make a wide range of materials. 13800 South Lakes Drive, Charlotte, N.C., U.S.A. Ion-conducting membranes can be any material.
  • Non-permselective membranes include
  • perm-selective membranes include SELEMION AMETM and
  • electrodeionization unit 100 is identical to electrodeionization unit 10 illustrated in Figure 5.
  • First compartment 119a is defined by anion exchange membrane 30 and separator
  • separator 120 prevents mixing of liquids in first compartment 119a with
  • first compartment 119a and second compartment 119b under the influence of the applied
  • An electrodeionization device (effective area 507 cm 2 [width ( ⁇ diluting and
  • compartment spacer length 39 cm] x 30 cell pairs
  • a filter press type 39 cm] x 30 cell pairs
  • electrodeionization stack having diluting compartments alternating with concentrating
  • each of these compartments being bounded by a cation exchange
  • diluting compartment spacer frames made of
  • concentrating compartments consisted of a sequential layered arrangement of two layers
  • MF membrane #1147027 from Osmonics, Minnetonka, MN, U.S.A.
  • the middle layer functioned as a
  • the diluting compartments were packed with cation exchange resin and anion
  • Feed water to be purified was prepared comprising of 1 ppm hardness as CaCO 3
  • the feed water to be purified was passed in a downward direction through the
  • electrodeionization device was set at 4.3 Amps using a rectifier capable of a maximum output voltage of 600 Volts. During operation, the stack voltage and product water
  • the present invention provides a number important advantages.
  • the concentrate As a further means of impeding transport of metallic cations to the concentrate compartment side surface of the anion exchange membranes, the concentrate
  • compartment may be divided into first and second compartments by a porous diaphragm
  • the diaphragm or membrane effectively reduces the rate of transport of scale-forming metallic cations from the compartment proximate the cation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Urology & Nephrology (AREA)
  • Molecular Biology (AREA)
  • Analytical Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
PCT/CA1999/000882 1998-10-16 1999-09-24 Method and apparatus for preventing scaling in electrodeionization units Ceased WO2000023382A1 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
DE69912985T DE69912985T2 (de) 1998-10-16 1999-09-24 Verfahren zur kesselsteinverhinderung in elektroentionisierungsanlagen
IL14248899A IL142488A0 (en) 1998-10-16 1999-09-24 Method and apparatus for preventing scaling in electrodeionization units
BR9914586-3A BR9914586A (pt) 1998-10-16 1999-09-24 Processo para a inibição de formação de incrustação em uma unidade de eletrodeionização para a deionização de água, e, unidade de eletrodeionização para a deionização de água
MXPA01003822A MXPA01003822A (es) 1998-10-16 1999-09-24 Metodo y aparato para prevenir la formacion de incrustaciones en unidades de elelctrodesionizacion.
EP99945796A EP1133449B1 (en) 1998-10-16 1999-09-24 Method for preventing scaling in electrodeionization units
AU58438/99A AU5843899A (en) 1998-10-16 1999-09-24 Method and apparatus for preventing scaling in electrodeionization units
AT99945796T ATE254581T1 (de) 1998-10-16 1999-09-24 Verfahren zur kesselsteinverhinderung in elektroentionisierungsanlagen
CA2347473A CA2347473C (en) 1998-10-16 1999-09-24 Method and apparatus for preventing scaling in electrodeionization units
JP2000577118A JP4805455B2 (ja) 1998-10-16 1999-09-24 電気脱イオンユニットにおけるスケール発生を防ぐ方法および装置

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/174,248 US6149788A (en) 1998-10-16 1998-10-16 Method and apparatus for preventing scaling in electrodeionization units
US09/174,248 1998-10-16

Publications (1)

Publication Number Publication Date
WO2000023382A1 true WO2000023382A1 (en) 2000-04-27

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA1999/000882 Ceased WO2000023382A1 (en) 1998-10-16 1999-09-24 Method and apparatus for preventing scaling in electrodeionization units

Country Status (12)

Country Link
US (1) US6149788A (https=)
EP (1) EP1133449B1 (https=)
JP (1) JP4805455B2 (https=)
CN (2) CN1323279A (https=)
AT (1) ATE254581T1 (https=)
AU (1) AU5843899A (https=)
BR (1) BR9914586A (https=)
CA (1) CA2347473C (https=)
DE (1) DE69912985T2 (https=)
IL (1) IL142488A0 (https=)
MX (1) MXPA01003822A (https=)
WO (1) WO2000023382A1 (https=)

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US6296751B1 (en) 1999-09-13 2001-10-02 Leon Mir Electrodeionization apparatus with scaling control
WO2004071968A1 (ja) 2003-02-14 2004-08-26 Kurita Water Industries Ltd. 電気脱イオン装置及びその運転方法
EP2390236A4 (en) * 2009-01-23 2012-10-10 Univ Tsinghua WASTEWATER TREATMENT METHOD AND 8209 DEVICE FOR SIMULTANEOUS ELECTRIC POWER GENERATION AND DESALINATION

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CA2347473A1 (en) 2000-04-27
BR9914586A (pt) 2001-07-03
JP2002527238A (ja) 2002-08-27
MXPA01003822A (es) 2003-07-21
CN101195081A (zh) 2008-06-11
DE69912985D1 (de) 2003-12-24
EP1133449A1 (en) 2001-09-19
EP1133449B1 (en) 2003-11-19
US6149788A (en) 2000-11-21
IL142488A0 (en) 2002-03-10
ATE254581T1 (de) 2003-12-15
JP4805455B2 (ja) 2011-11-02
AU5843899A (en) 2000-05-08
CN101195081B (zh) 2011-08-31
DE69912985T2 (de) 2004-09-02
CA2347473C (en) 2010-05-25
CN1323279A (zh) 2001-11-21

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