Co-producing apparatus for salt and fresh water and co-producing method of the same

1. A co-producing apparatus for salt and fresh water comprising:

a raw water supply line that supplies raw water;

a pretreatment apparatus that filters a turbid content of the raw water so as to produce pretreated water;

an electrodialyzer that electrodialyzes the pretreated water so as to produce concentrated brine and diluted brine;

an evaporator that evaporates the concentrated brine so as to produce condensed water and evaporated water;

a dryer that produces salt by drying the condensed water;

an acid adding unit that adds acid to the diluted brine;

a reverse osmosis membrane apparatus having a reverse osmosis membrane that produces (i) fresh water that is permeated water obtained by removing a salt content from the diluted brine to which the acid is added and (ii) salt-enriched membrane separation concentrated water;

a recycle line that brings a part of the salt-enriched membrane separation concentrated water back to a rear flow side of the pretreatment apparatus as a recycling membrane separation concentrated water;

a water discharge line that discharges a rest part of the salt-enriched membrane separation concentrated water into a sea area as a discharging membrane separation concentrated water;

an ion concentration meter that detects ion concentrations of divalent ions and SO 4 2− ions of the recycling membrane separation concentration water, the ion concentration meter being provided on the recycle line;

a control apparatus that controls to adjust a ratio between a discharging amount of the discharging membrane separation concentrated water to be discharged into a sea area and a supplying amount of the raw water of the raw water supply line in response to the detected ion concentrations so that these ion concentrations are equal to or less than a saturation concentration of gypsum, wherein

produced water is obtained by combining the evaporated water supplied from the evaporator with the permeated water supplied from the reverse osmosis membrane apparatus.

2. A co-producing apparatus for salt and fresh water comprising:

a raw water supply line that supplies raw water;

a pretreatment apparatus that filters a turbid content of the raw water so as to produce pretreated water;

an electrodialyzer that electrodialyzes the pretreated water so as to produce concentrated brine and diluted brine;

an evaporator that evaporates the concentrated brine so as to produce condensed water and evaporated water;

a dryer that produces salt by drying the condensed water;

an acid adding unit that adds acid to the diluted brine;

a nanofiltration membrane separation apparatus that removes divalent ions from the diluted brine to which the acid is added so as to produce treated water and membrane separation concentrated water;

a reverse osmosis membrane apparatus having a reverse osmosis membrane that produces (i) fresh water that is permeated water obtained by removing a salt content of the treated water supplied from the nanofiltration membrane separation apparatus and (ii) salt-enriched membrane separation concentrated water;

a recycle line that brings a total amount of the salt-enriched membrane separation concentrated water supplied from the reverse osmosis membrane apparatus back to a rear flow side of the pretreatment apparatus as recycling membrane separation concentrated water;

a water discharge line that discharges a total amount of the membrane separation concentrated water supplied from the nanofiltration membrane separation apparatus into a sea area;

an ion concentration meter that detects ion concentrations of divalent ions and SO 4 2− ions of the recycling membrane separation concentrated water;

a control apparatus that controls to adjust a ratio between a discharging amount of the membrane separation concentrated water to be discharged into a sea area and a supplying amount of the raw water of the raw water supply line in response to the detected ion concentrations so that these ion concentrations are equal to or less than a saturation concentration of gypsum, wherein

produced water is obtained by combining the evaporated water supplied from the evaporator with the permeated water supplied from the reverse osmosis membrane apparatus.

3. The co-producing apparatus for salt and fresh water according to claim 2 , further comprising a bypass line through which, after the acid is added to the diluted brine supplied from the electrodialyzer, a part of the acid-added diluted brine bypasses the nanofiltration membrane separation apparatus, to be supplied to the reverse osmosis membrane apparatus.

4. A co-producing method for salt and fresh water comprising:

supplying raw water;

filtering a turbid content of the raw water, so as to obtain pretreated water;

electrodialyzing the pretreated water so as to obtain diluted brine and concentrated brie;

evaporating the concentrated brine to produce salt;

adding acid to the diluted brine;

removing a salt content from acid-added diluted brine to obtain (i) fresh water that is permeated water and (ii) salt-enriched membrane separation concentrated water;

bringing a part of the salt-enriched membrane separation concentrated water as recycling membrane separation concentrated water to the pretreated water;

discharging a rest part of the salt-enriched membrane separation concentrated water into a sea area as a discharging membrane separation concentrated water;

detecting ion concentration of divalent ions and SO 4 2− ions of the recycling membrane separation concentrated water; and

adjusting a ratio between a discharging amount of the discharging membrane separation concentrated water to be discharged into a sea area and a supplying amount of the raw water in response to the detected ion concentrations so that these ion concentrations are equal to or less than a saturation concentration of gypsum, wherein

produced water is obtained by combining the evaporated water with the permeated water.

5. A co-producing method for salt and fresh water comprising:

supplying raw water;

filtering a turbid content of the raw water so as to obtain pretreated water;

electrodialyzing the pretreated water so as to obtain concentrated brine and diluted brine;

evaporating the concentrated brine so as to obtain condensed water and evaporated water;

drying the condensed water so as to obtain salt;

adding acid to the diluted brine;

removing divalent ions from the diluted brine to which the acid is added so as to obtain treated water and membrane separation concentrated water;

producing (i) fresh water that is permeated water obtained by removing a salt content of the treated water and (ii) salt-enriched membrane separation concentrated water;

brings a total amount of the salt-enriched membrane separation concentrated water to the pretreated water as recycling membrane separation concentrated water;

discharging a total amount of the membrane separation concentrated water into a sea area;

detecting ion concentrations of divalent ions and SO 4 2− ions of the recycling membrane separation concentrated water;

adjusting a ratio between a discharging amount of the membrane separation concentrated water to be discharged into a sea area and a supplying amount of the raw water in response to the detected ion concentrations so that these ion concentrations are equal to or less than a saturation concentration of gypsum, wherein

produced water is obtained by combining the evaporated water supplied from the evaporator with the permeated water supplied from the reverse osmosis membrane apparatus.