WATER TREATMENT USING A BIPOLAR MEMBRANE
BACKGROUND OF THE INVENTION
Related Application
[0001] US Application 12/123,521, filed May 20, 2008, and assigned to General
Electric Company, which is herein incorporated by reference.
Field of the Invention
[0002] This invention is related to the use of an electrolysis device for water
treatment.
Description of Related Art
[0003] The presence of scale forming species in aqueous systems, such as brackish
water and cooling tower make up or blowdown, lead to an increase in system
maintenance and a decrease in system yield. Accordingly, a need exists to decrease the
presence of scale forming species in aqueous systems.
SUMMARY OF THE INVENTION
[0004] One embodiment of the present invention concerns a method of water
treatment comprising: providing an electrolysis device comprising an electrolysis vessel;
providing feed streams to the first salt water chamber of the vessel, second salt water
chamber of the vessel, acidic chamber of the vessel, and alkalic chamber of the vessel,
the acidic chamber producing an acidic solution and the alkalic chamber producing an
alkalic solution; directing at least a portion of the contents of the first and second salt
water chambers into a precipitation tank; directing at least a portion of the alkalic solution
into the precipitation tank, thereby increasing the pH in the precipitation tank to produce
precipitate; and removing the precipitate from the precipitation tank.[0005] Another embodiment of the present invention concerns an electrolysis device
comprising a pair of electrodes arranged in the electrolysis vessel, serving as a positive
electrode and a negative electrode, respectively; and a cell unit arranged between the
positive and negative electrodes, the cell unit comprising a bipolar membrane element
and at least one cation exchangeable membrane, the bipolar membrane element having a
cation exchangeable side and an anion exchangeable side, the cation exchangeable side
being closer to the negative electrode than the anion exchangeable side, the at least one
cation exchangeable membrane being arranged between the anion exchangeable side of
the bipolar membrane element and the positive electrode, so as to define an alkalic
chamber between the bipolar membrane element and the cation exchangeable membrane;
wherein the cation exchangeable membrane is selective.
BRIEF DESCRIPTION OF THE DRAWINGS
[0006] These and other aspects of the invention will be understood from the
description and claims herein, taken together with the drawings showing details of
construction and illustrative embodiments, wherein:
[0007] Fig. 1 schematically illustrates one embodiment of the bipolar membrane;
[0008] Fig. 2 schematically illustrates a method of operating bipolar membrane of Fig.
i ;
[0009] Fig. 3 schematically illustrates a method of operating bipolar membrane of Fig.
i ;
[0010] Fig. 4 schematically illustrates a method of operating bipolar membrane of Fig.
i ;
[0011] Fig. 5 schematically illustrates a method of operating bipolar membrane of Fig.
i ;
[0012] Fig. 6 schematically illustrates a method of operating bipolar membrane of Fig.
i ;
[0013] Fig. 7 schematically illustrates a method of operating bipolar membrane of Fig.
1; and[0014] Fig. 8 schematically illustrates a method of operating bipolar membrane of Fig.
1.
DETAILED DESCRIPTION OF THE INVENTION
[0015] Approximating language, as used herein throughout the specification and
claims, may be applied to modify any quantitative representation that could permissibly
vary without resulting in a change in the basic function to which it is related.
Accordingly, a value modified by a term or terms, such as "about", is not limited to the
precise value specified. In at least some instances, the approximating language may
correspond to the precision of an instrument for measuring the value. Range limitations
may be combined and/or interchanged, and such ranges are identified and include all the
sub-ranges stated herein unless context or language indicates otherwise. Other than in the
operating examples or where otherwise indicated, all numbers or expressions referring to
quantities of ingredients, reaction conditions and the like, used in the specification and
the claims, are to be understood as modified in all instances by the term "about".
[0016] "Optional" or "optionally" means that the subsequently described event or
circumstance may or may not occur, or that the subsequently identified material may or
may not be present, and that the description includes instances where the event or
circumstance occurs or where the material is present, and instances where the event or
circumstance does not occur or the material is not present.
[0017] As used herein, the terms "comprises", "comprising", "includes", "including",
"has", "having", or any other variation thereof, are intended to cover a non-exclusive
inclusion. For example, a process, method, article or apparatus that comprises a list of
elements is not necessarily limited to only those elements, but may include other
elements not expressly listed or inherent to such process, method, article, or apparatus.
[0018] The singular forms "a", "an", and "the" include plural referents unless the
context clearly dictates otherwise.
[0019] Cooling towers are widely used in industries to remove heat in processes, such
as oil refinery, chemical processes, and power generation plants. Cooling towers are also
used in the HVAC systems common in commercial, institutional, and hospital buildings.Water consumption in cooling tower operation constitutes the largest water withdrawal
from natural water sources in many countries. Water scarcity has become an increasing
concern worldwide. According to the data published by Global environment outlook, 5%
of population was facing water scarcity problems in 2000, mainly in the middles east
area. However, by year 2030, nearly half of world population will be water stressed.
[0020] In addition to the limited water resources, environment regulation becomes
increasingly restricted to disposal of industrial wastewaters. Cost of treating wastewater
before discharge to environment is continuously increased in recent years.
[0021] Water shortage worldwide and stringent environment regulations have led to
increasing water conservation effort in all industries. Inevitably, it has significant impact
on industry water use, especially on huge water consumption industries. Cooling water
system conservation efforts have focused on replacing fresh water with treated municipal
effluent, reusing plant wastewater, and reducing water discharge by operating at higher
cycles of concentration, such as greater than about 7 cycles.
[0022] With increasing cycles of concentration, the tendency for deposition increased
due to high concentration of Ca, alkalinity, Si0 2, silt, Fe, Al, etc. Likewise, the tendency
for corrosion increased with increasing cycles due to high conductivity and high
concentration of CI and SO4
2 .
[0023] Common approach to treat cooling towers operating at high cycles is to add acid
to reduce alkalinity, operating cooling towers at lower pH, therefore, decreasing the
tendency of deposition or precipitation in cooling systems. This usually requires adding a
high dose of chemicals such as anionic polymers and corrosion inhibitors to cooling
towers. However, handling and storage of strong acid posed a danger to workers and
environment, especially in commercial and institutional buildings. Increasing usage of
chemicals also results in increasing overall cost of the treatment.
[0024] In one embodiment, the present invention is directed toward a method of treating
water from cooling towers operating at a high cycle of concentration using an electrolysis
device, such as a bipolar membrane or its combination with a nanofiltration unit. Cooling
tower water is provided to the electrolysis device. An acidic solution generated from the
electrolysis device is added to cooling towers to reduce alkalinity and pH. An alkalicsolution generated from the electrolysis device is added to a portion of cooling tower
blowdown stream in a separation apparatus to precipitate calcium, silica and other scale
forming species. The water after precipitates removal in the separation apparatus is
softened and returned to cooling tower. This method allows cooling tower to operate at
high cycles of concentration and/or achieve zero liquid discharge, thus significantly
reducing water consumption and water treatment chemical usage.
[0025] Referring to Fig. 1, a first embodiment of the electrolysis device 2 for
producing an acidic solution and alkalic solution includes a pair of electrodes respectively
acting as a positive electrode 2 1 and a negative electrode 22, at least one cell
unit 23 between the positive and negative electrodes 21, 22, and a vessel 24 for housing
the electrodes 21, 22 and the cell unit 23 therein. The positive and negative
electrodes 21, 22 respectively connect with an anode and a cathode of a DC power
supply 25. The vessel 24 includes at least a first inlet 243, second inlet 244, third inlet,
245, and fourth inlet 246 for inducing a feed stream to flow through the electrolysis
device 2. The cell unit 23 includes at least one alkalic chamber 236 and at least one
acidic chamber 235 defined between ion exchangeable membranes, which will be
discussed in detail below.
[0026] The cell unit 23 of the vessel 24 of electrolysis device 2 according to the first
embodiment, shown in FIG. 1, comprises a bipolar membrane element 230, a cation
exchangeable membrane 231, and an anion exchangeable membrane 232. The bipolar
membrane element 230 has a cation exchangeable side 233 and an anion exchangeable
side 234, and is used as a water splitter. The cation exchangeable side 233 of the bipolar
membrane element 230 is closer to the positive electrode 2 1 than the anion exchangeable
membrane 232. The cation exchangeable membrane 231 is arranged between the anion
exchangeable side 234 and the positive electrode 21. The anion exchangeable
membrane 232 is arranged between the cation exchangeable side 233 and the negative
electrode 22.
[0027] A direct current from the power supply 25 flows through the bipolar membrane
element 230 causing the water to split with OH ions being produced on the anion
exchangeable side 234 and a corresponding number of H+ ions being produced on thecation exchangeable side 233 of the bipolar membrane element 230. The generated
OH and H+ ions are prevented from moving further by the cation exchangeable
membrane 231 and the anion exchangeable membrane 232, respectively.
[0028] Cation exchangeable membrane 231 is selective and only passes univalent
cationic ions. Anion exchangeable membrane 232 is selective and only passes univalent
anionic ions. Accordingly, Na+ ions from the salt water received by second inlet 244
move through cation exchangeable membrane 231 toward the negative electrode 22,
while Ca , Mg , Ba , F Fe , and Α do not move through cation exchangeable
membrane 231. Further, CI ions from the salt water received by first inlet 243 move
through anion exchangeable membrane 232 toward the positive electrode 21, while C0 3
, S0 4
2 and PO4
3 do not move through the anion exchangeable membrane 232.
[0029] Thus an alkalic chamber 236 is defined between the bipolar membrane
element 230 and the cation exchangeable membrane 231, and an acidic chamber 235 is
defined between the bipolar membrane element 230 and the anion exchangeable
membrane 232.
[0030] A first salt water chamber 237 is defined between negative electrode 22 and
anion exchangeable membrane 232. A second salt water chamber 238 is defined between
positive electrode 2 1 and cation exchangeable membrane 231.
[0031] A first inlet 243 provides a feed stream to the first salt water chamber 237, a
second inlet 244 provides a feed stream to the second salt water chamber 238, a third
inlet 245 provides a feed stream to the acidic chamber 235, and a fourth inlet 244
provides a feed stream to the alkalic chamber 236. The feed streams provided to first salt
water chamber 237 and second salt water chamber 238 may be comprised of at least one
of cooling tower make up water, cooling tower blow down water, or low quality water
[0032] The vessel 24 further includes an acidic outlet 24l and an alkalic
outlet 242 respectively for the alkalic solution of alkalic chamber 236 and the acidic
solution of acidic chamber 235 to flow out of. The vessel 24 also includes a first salt
water outlet 247 and a second salt water outlet 248 respectively for the salt water of first
salt water chamber 237 and second salt water chamber 238 to flow out of.[0033] The feed stream entering the acidic chamber 235 through inlet 245 can be one
or both of pure water or the acidic solution exiting acidic outlet 241 of the vessel 24. The
feed stream entering alkalic chamber 236 through inlet 246 can be one or both of pure
water or the alkalic solution exiting alkalic outlet 242 of vessel 24.
[0034] The alkalic solution produced at alkalic outlet 242 can be used to create a high
pH environment to precipitate hardness and other species in aqueous systems, such as
CaC0 3, CaMg(C0 3)
2, Ca3(P0 4)
2,Ca5(P0 4)
3OH, CaS0 4, Fe(OH)
3, Al(OH)
3, MgSi0 3 etc.
The acidic solution produced in acidic chamber 235 can be used to adjust pH of cooling
tower water and clean hardness off membranes or electrodes in the vessel 24.
[0035] The bipolar membrane element 230 has a water splitting feature to split water
directly into H+ and OH .
[0036] The application of the bipolar membrane element 230 greatly improves the
efficiency of the electrolysis device 2 for producing alkalic solution and acidic solution
from the water. The bipolar membrane element 230 may be a bipolar membrane which
includes a cation exchangeable layer and an anion exchangeable layer, or a bipolar
module formed by a combination of anion and cation exchangeable membranes which
functions as a bipolar membrane.
[0037] In one embodiment, the positive and negative electrodes 21, 22 are made from
highly porous carbon materials selected from any of activated carbon, carbon black,
carbon nanotubes, graphite, carbon fiber, carbon cloth, carbon aerogel, or combination
thereof. Surface area of the carbon material is in a range of from about 500 to 2000
square meters per gramme as measured by nitrogen adsorption BET method high porous
positive and negative electrodes 21, 22 each have a shape, size or configuration that is a
plate, a block, a cylinder, or a sheet. It is also anticipated that positive and negative
electrodes 21, 22 can be made of any metal or porous material deemed suitable by a
person having ordinary skill in the art, such as activated carbon.
Θ 038] Fig. 2 discloses one embodiment in which electrolysis device 2 is used to
generate acid solution for cooling tower water pH adjustment or cleaning of electrolysis
device 2 and to generate base for hardness precipitation. In this configuration, the output
of salt water tank 301 is provided as a feed stream to said first salt water chamber 237and second salt water chamber 238 of vessel 24. Salt water tank 301 can contain one or
more of cooling tower make up water, cooling tower blow down water, or low quality
water. Low quality water is any water that needs to be treated to soften and/or remove
undesirable ion species, such as brackish water. Water is provided as a feed stream to the
acidic chamber 235 and alkalic chamber 236. The output of acidic chamber 235 is
provided to cooling towers. The output of alkalic chamber 236 is provided to
precipitation tank 304, and the output of the first and second salt water chambers 237 and
238 is also provided to the precipitation tank 304. Accordingly, the addition of the
alkalic solution from alkalic chamber 236 into precipitation tank 304 increases the pH in
precipitation tank 304 to a desired value to precipitate metal salts and metal hydroxides,
such as CaCC"3, MgCCh, CaS0 4, Mg(OH)
2, etc. After the precipitate is removed from
precipitation tank 304, the treated water from precipitation tank 304 is provided to a
water storage tank or to cooling towers. In one embodiment, the desired pH value in
precipitation tank 304 after the addition of alkalic solution from electrolysis device 2 is
between about7 to 14, preferably between about 8 to 13 and more preferably between
about 9 to 12.
[0039] Further, as is shown in Fig. 3, it is also contemplated that in some
embodiments all or part of the acidic solution produced in acidic chamber 235 can be
returned to acidic chamber 235 as a feed stream. Further, all or part of the alkalic
solution produced in alkalic chamber 236 can be returned to alkalic chamber 236 as a
feed stream. This would allow for the concentration of the acid and base solutions to be
increased with time within acidic chamber 235 and alkalic chamber 236. Further, this
would allow for the pH within the precipitation tank 304 increases to enhance
precipitation.
[0040] Fig. 4 discloses another embodiment in which electrolysis device 2 is used to
generate an acidic solution for cooling tower water pH adjustment or cleaning of
electrolysis device and to generate a base solution for hardness precipitation. In this
embodiment, cooling tower blowdown is delivered to selective membrane 501, which
outputs a divalent ion stream that is provided to precipitation tank 502. Selective
membrane 501 may be a nano filtration unit. The divalent ion stream contains one ormore divalent ions, such as Ca +, Mg +, Ba +, Fe +' Fe +, Al +, C0 3 , S0 4 and P0 4 , etc.
Selective membrane 501 outputs a univalent ion stream that is provided to the first and
second salt water chambers 237 and 238 of vessel 24. The univalent ion stream contains
one or more univalent ions, such as Na+, CI , etc. Further, a water feed stream is provided
to the acidic chamber 235 and alkalic chamber 236 of vessel 24.
[0041] The alkalic solution output of the alkalic chamber 236 is provided to the
precipitation tank 502, which increases the pH in precipitation tank 502 to a desired value
to precipitate metal salts and metal hydroxides, such as CaC0 3, MgC0 3, CaS0 4,
Mg(OH)
2, etc. In one embodiment, the desired pH value in precipitation tank 304 after
the addition of alkalic solution from vessel 24 is between about 7 to 14, preferably
between about 8 to 13 and more preferably between about 9 to 12.
[0042] The precipitates are then removed from precipitation tank 502 and the
remaining treated water contained in precipitation tank 502 is used as cooling tower make
up water or for other industrial processes. The output of the first and second salt water
chambers 237 and 238 is combined with the remaining treated water from the
precipitation tank 302 as cooling tower make up water or for other industrial processesv
The acidic solution output of the acidic chamber 235 can be used to adjust pH of cooling
tower water and/or adjust the pH of treated water stream exiting from precipitation tank
502, and to clean membranes of vessel 24. Returning the remaining water from
precipitation tank 502 to the cooling tower reduces water consumption and reduces or
eliminates the waste water discharged to a sewer or river. Further, the use of high quality
water in the cooling tower reduces the amount of chemicals required to treat the water in
the cooling tower, thus reducing disposal cost and impact on the environment.
[0043] Further, as is shown in Fig. 5, it is also contemplated that in some
embodiments all or part of the acidic solution output of acidic chamber 235 can be
returned to acidic chamber 235 as a feed stream. Further, all or part of the alkalic
solution output of alkalic chamber 236 can be returned to alkalic chamber 236 as a feed
stream. This would allow for the concentration of acid and base solutions to be increased
with time within acidic chamber 235 and alkalic chamber 236. Additionally, the output
of salt chambers 237 and 238 is combined with the remaining treated water from theprecipitation tank after precipitate removal as cooling tower make up water or for other
industrial processes.
[0044] Fig. 6 discloses another embodiment in which electrolysis device 2 is used to
generate acidic solution for cooling tower water pH adjustment, the cleaning of
electrolysis device 2, and/or to generate base for hardness precipitation. In this
embodiment, a feed stream of low quality water, such as brackish water, is delivered to
selective membrane 601, which outputs a divalent ion stream that is provided to
precipitation tank 602. However, it is contemplated that the feed stream can be
comprised of at least one of cooling tower make up water, cooling tower blow down, or
low quality water. The divalent ion stream contains one or more divalent ions, such as
Ca +, Mg +, Ba +, Fe +' Fe +, Al +, C0 3 , S0 4 , P0 4
3, etc. Selective membrane 601
outputs a univalent ion stream that is provided to the first and second salt water chambers
237 and 238 of electrolysis device 2. Selective membrane 601 may be a nanofiltration
unit. The univalent ion stream contains one or more univalent ions, such as Na+, CI , etc.
Further, a water feed stream is provided to the acidic chamber 235 and alkalic chamber
236 of vessel 24.
[0045] The output of the alkalic chamber 236 is provided to the precipitation tank 602,
which increases the pH in precipitation tank 602 to a desired value to precipitate Ca and
Mg salts and metal hydroxides. In one embodiment, the desired pH value in precipitation
tank 602 after the addition of alkalic solution from vessel 24 is between about 7 to 14,
preferably between about 8 to 13 and more preferably between about 9 to 12. The
precipitates are then removed from precipitation tank 602 and the remaining treated water
contained in precipitation tank 602 is used as cooling tower make up water or for other
industrial processes. The output of first and second salt water chambers 237 and 238 is
combined with the remaining treated water from the precipitation tank and used as
cooling tower make up water or for other industrial processes. The acidic solution output
of the acidic chamber 235 can be used to adjust the pH of cooling tower water, adjust the
pH of the treated water stream exiting from precipitation tank 602, and/or clean
membranes of vessel 24.[0046] Further, as is shown in Fig. 7, it is also contemplated that in some embodiments
all or part of the output of acidic chamber 235 can be returned to acidic chamber 235 as a
feed stream. Further, all or part of the output of alkalic chamber 236 can be returned to
alkalic chamber 236 as a feed stream. This would allow for the concentration of acid
solution and base solution to be increased with time within acidic chamber 235 and
alkalic chamber 236. The output of first salt water chambers 237 and 238 is combined
with the remaining treated water from the precipitation tank and used as cooling tower
make up water or for other industrial processes.
[0047] Turning to Fig. 8, in one embodiment of this invention, a first portion of
blowdown from a cooling tower operating at a high cycle of concentration, greater than
about 7 cycles, and pure water are provided to an electrolysis unit. The electrolysis unit
uses the first portion of blowdown and pure water to generate an acidic solution in acid
chamber 235, an alkalic solution in alkalic chamber 236, and a salt water solution in first
and second chambers 237 and 238. The acidic solution is provided to the cooling tower
to reduce the alkalinity and pH of the water circulating through the cooling tower. The
alkalic solution is mixed with a second portion of blowdown in precipitation tank 702 to
precipitate and remove calcium and other scaling forming species from the second
portion of blowdown, thereby softening the second portion of blowdown. The softened
second portion of blowdown is then returned to the cooling tower as make up water.
[0048] In one embodiment, the blowdown is filtered by a nanofiltration unit 701 after
leaving the cooling tower. After nanofiltration, the first portion of blowdown is
comprised of one or more univalent ions and the second portion of blowdown is
comprised of one or more divalent ions. In some embodiments, the salt water solution is
added to the softened second portion of blowdown and returned to the cooling tower as
makeup water.
[0049] While this invention has been described in conjunction with the specific
embodiments described above, it is evident that many alternatives, combinations,
modifications and variations are apparent to those skilled in the art. Accordingly, the
preferred embodiments of this invention, as set forth above are intended to be illustrative
only, and not in a limiting sense. Various changes can be made without departing fromthe spirit and scope of this invention. Therefore, the technical scope of the present
invention encompasses not only those embodiments described above, but also all that fall
within the scope of the appended claims.
[0050] This written description uses examples to disclose the invention, including the
best mode, and also to enable any person skilled in the art to practice the invention,
including making and using any devices or systems and performing any incorporated
processes. The patentable scope of the invention is defined by the claims, and may
include other examples that occur to those skilled in the art. These other examples are
intended to be within the scope of the claims if they have structural elements that do not
differ from the literal language of the claims, or if they include equivalent structural
elements with insubstantial differences from the literal language of the claims.What is claimed is:
CLAIMS
1. A method of cooling tower water treatment comprising:
obtaining a first and a second portion of blowdown from a cooling tower
operating at a high cycle of concentration;
obtaining pure water;
providing said first portion of blowdown and pure water to an electrolysis
unit;
obtaining an acidic solution, an alkalic solution, and a salt water solution
from said electrolysis unit;
providing said acidic solution to the cooling tower to reduce the alkalinity
and pH of the water circulating through the cooling tower;
mixing said alkalic solution and said second portion of blowdown in a
precipitation tank to soften said second portion of blowdown, removing resulting
precipitate from said precipitation tank; and
providing said softened second portion of blowdown in said precipitation
tank to said cooling tower as makeup water.
2. A method of water treatment comprising:
providing an electrolysis device comprising:
an electrolysis vessel;
a pair of electrodes arranged in the electrolysis vessel, the pair of
electrodes respectively serving as a positive electrode and a
negative electrode; and
a cell unit arranged between the positive and negative electrodes,
the cell unit comprising a bipolar membrane element and at least
one cation exchangeable membrane, the bipolar membrane element
having a cation exchangeable side and an anion exchangeable side,
the cation exchangeable side being closer to the negative electrode
than the anion exchangeable side, said at least one cationexchangeable membrane being arranged between the anion
exchangeable side of the bipolar membrane element and the
positive electrode, so as to define an alkalic chamber between the
bipolar membrane element and the cation exchangeable membrane,
said cation exchangeable membrane is selective;
an anion exchangeable membrane between the negative electrode
and the cation exchangeable side of the bipolar membrane element,
an acidic chamber being defined between the anion exchangeable
membrane and the bipolar membrane element, said anion
exchangeable membrane is selective;
a first salt water chamber defined between said negative electrode
and anion exchangeable membrane, a second salt water chamber
defined between said positive electrode and said cation
exchangeable membrane; and
a first inlet providing a feed stream to said first salt water chamber,
a second inlet providing a feed stream to said second salt water
chamber, a third inlet providing a feed stream to said acidic
chamber, and a fourth inlet providing a feed stream to said alkalic
chamber;
providing feed streams to said first salt water chamber, second salt water
chamber, acidic chamber, and alkalic chamber, said acidic chamber
producing an acidic solution and said alkalic chamber producing an alkalic
solution;
directing at least a portion of the contents of said first and second salt
water chambers into a precipitation tank; directing at least a portion of the
alkalic solution into said precipitation tank, thereby increasing the pH in
said precipitation tank to produce precipitate; and
removing said precipitate from said precipitation tank.3. The method of claim 2, wherein the pH in said precipitation tank is
increased to about 7-14.
4. The method of claim 3, wherein the feed stream provided to said acidic
and alkalic chambers is H20 , and the feed stream provided to said first salt water
chamber and said second salt water chamber is comprised of at least one of cooling tower
make up water, cooling tower blow down water, or low quality water.
5. The method of claim 4, wherein the treated water in said precipitation tank
is returned to said cooling tower after said precipitate is removed from said precipitation
tank.
6. The method of claim 4, wherein the treated water in said precipitation tank
is provided to a water storage tank after said precipitate is removed from said
precipitation tank.
7. The method of claim 4, wherein the acidic solution is provided to said
cooling tower for pH adjustment or used to adjust the pH of the treated water exiting the
precipitation tank after the precipitate is removed.
8. The method of claim 4, wherein the acidic solution is used to clean the
membranes of said vessel.
9. The method of claim 4, wherein at least a portion of said acidic solution is
returned to said acidic chamber as a feed stream.
10. The method of claim 4, wherein at least a portion of said alkalic solution is
returned to said alkalic chamber as a feed stream.11. The method of claim 3, further comprising providing a selective
membrane, said selective membrane receives a feed stream comprised of at least one of
cooling tower make up water, cooling tower blow down, or low quality water;
said selective membrane outputs a divalent stream and a univalent stream;
wherein, said divalent stream is provided to said precipitation tank; said
univalent stream is provided to said first salt water chamber and said second salt water
chamber; and said acidic and alkalic chambers are provided with an H20 feed stream.
12. The method of claim 11, wherein the treated water in said precipitation
tank is returned to said cooling tower after said precipitate is removed from said
precipitation tank.
13. The method of claim 11, wherein the treated water in said precipitation
tank is provided to a water storage tank after said precipitate is removed from said
precipitation tank.
14. The method of claim 11, wherein the acidic solution is provided to said
cooling tower for pH adjustment or to adjust the pH of the treated water exiting the
precipitation tank after the precipitate is removed.
15. The method of claim 11, wherein the acidic solution is used to clean the
membranes of said vessel.
16. The method of claim 11, wherein at least a portion of said acidic solution
is returned to said acidic chamber as a feed stream.
17. The method of claim 11, wherein at least a portion of said alkalic solution
is returned to said alkalic chamber as a feed stream.18. The method of claim 11, wherein at least a portion of the output of the first
and second salt chambers is combined with the remaining treated water from the
precipitation tank and provided as make up water to the cooling tower.
19. An electrolysis device for water treatment comprising:
an electrolysis vessel;
a pair of electrodes arranged in the electrolysis vessel, the pair of
electrodes respectively serving as a positive electrode and a negative electrode; and
a cell unit arranged between the positive and negative electrodes, the cell
unit comprising a bipolar membrane element and at least one cation exchangeable
membrane, the bipolar membrane element having a cation exchangeable side and an
anion exchangeable side, the cation exchangeable side being closer to the negative
electrode than the anion exchangeable side, said at least one cation exchangeable
membrane being arranged between the anion exchangeable side of the bipolar membrane
element and the positive electrode, so as to define an alkalic chamber between the bipolar
membrane element and the cation exchangeable membrane;
said electrolysis vessel further comprising an anion exchangeable
membrane between the negative electrode and the cation exchangeable side of the bipolar
membrane element, an acidic chamber being defined between the anion exchangeable
membrane and the bipolar membrane element;
wherein said anion and cation exchangeable membranes are selective;
wherein said alkalic chamber produces an alkalic solution and said acidic
chamber produces an acidic solution.