Treating cooling water in iron production facilities, and associated systems, devices, and methods
Treating cooling water in industrial production facilities and associated systems, devices, and methods are disclosed herein. The system can comprise a cooling tower with a first and second cell, each having a housing to receive return water and a sump below to maintain supply water configured to directly contact molten metal. The system includes an inlet and an inlet line to provide return water to the cooling tower and an outlet and an outlet line to direct supply water back to the industrial production facility. The inlet, outlet, and cooling tower form a closed-loop network. Additionally, a blowdown line is fluidically coupled to the outlet to divert a portion of the supply water away from the closed-loop network.
1. A system for treating cooling water in an industrial production facility, the system comprising:
a cooling tower including a first cell and a second cell, each of the first and second cells including:
a housing positioned to receive a return water, and
a sump below the housing and configured to maintain a level of a supply water, wherein, in operation, (i) the supply water is in direct contact with molten metal from the industrial production facility, and (ii) the molten metal has a temperature of at least 1050° C. prior to contacting the supply water;
an inlet comprising an inlet line positioned to provide the return water to the cooling tower;
an outlet comprising an outlet line positioned to direct the supply water toward the industrial production facility, wherein the inlet, the outlet, and the cooling tower form a loop; and
a blowdown line fluidically coupled to the outlet and configured to direct a portion of the supply water away from the loop at a flow rate between 1,000 and 12,000 gallons per minute,
wherein the cooling tower is configured to operate for at least 12 hours continuously.
2. The system of claim 1 , wherein the return water is configured to include particles having a particle size between 0.1 micron and 20 microns.
3. The system of claim 1 , wherein the industrial production facility is configured to produce granulated metal via a granulator, and wherein the supply water of the outlet line directly contacts the granulated metal.
4. The system of claim 1 , further comprising a valve arrangement configured to isolate the return water and/or the supply water from the first cell.
5. The system of claim 4 , wherein the valve arrangement is a first valve arrangement, the system further comprising a second valve arrangement configured to isolate the return water and/or the supply water from the second cell.
6. The system of claim 1 , wherein the blowdown line is configured to direct the portion of the supply water to an external system not fluidically coupled to the cooling tower.
7. The system of claim 1 , further comprising a blowdown treatment system fluidically coupled to the blowdown line and including a flocculant supply configured to introduce a flocculant into the portion of the supply water.
8. The system of claim 1 , further comprising a cooling tower water treatment system fluidically coupled to a makeup line and including a dispersant supply configured to introduce a dispersant into a makeup water.
9. The system of claim 1 , wherein the cooling tower further comprises a third cell adjacent the second cell, a fourth cell adjacent the third cell, and a fifth cell adjacent the fourth cell.
10. The system of claim 1 , wherein each of the first and second cells further includes a basin below the sump and configured to collect settled solids from the supply water.
11. A system for treating cooling water in an industrial production facility, the system comprising:
a cooling tower including a basin, a first cell, and a second cell, each of the first and second cells including:
a housing positioned to receive a return water, and
a sump below the housing and configured to maintain a level of a supply water, wherein, in operation, (i) the supply water is in direct contact with molten metal from the industrial production facility, and (ii) the molten metal has a temperature of at least 1050° C. prior to contacting the supply water, wherein the housing and/or the sump of the cooling tower define a perimeter,
wherein the basin includes a first region associated with the first cell and a second region associated with the second cell, wherein the first region and/or the second region extends beyond the perimeter;
an inlet comprising an inlet line positioned to provide the return water to the cooling tower;
an outlet comprising an outlet line positioned to direct the supply water toward the industrial production facility, wherein the inlet, the outlet, and the cooling tower form a loop; and
a blowdown line fluidically coupled to the outlet and configured to direct a portion of the supply water away from the loop.
12. A system of for treating cooling water in an industrial production facility, the system comprising:
a cooling tower including a first cell and a second cell, each of the first and second cells including:
a housing positioned to receive a return water, and
a sump below the housing and configured to maintain a level of a supply water, wherein, in operation, (i) the supply water is in direct contact with molten metal from the industrial production facility, and (ii) the molten metal has a temperature of at least 1050° C. prior to contacting the supply water;
a trough below the sump of the cooling tower and extending across a length of the cooling tower including the first cell and the second cell;
an inlet comprising an inlet line positioned to provide the return water to the cooling tower;
an outlet comprising an outlet line positioned to direct the supply water toward the industrial production facility, wherein the inlet, the outlet, and the cooling tower form a loop; and
a blowdown line fluidically coupled to the outlet and configured to direct a portion of the supply water away from the loop.
13. A method for treating cooling water in an industrial production facility, the method comprising:
receiving a return water at a first cell and a second cell of a cooling tower;
cooling the return water via the cooling tower to produce a supply water in a sump of the cooling tower for at least 12 hours continuously;
directing a first portion of the supply water from the cooling tower to directly contact metal in the industrial production facility and produce the return water; and
directing a second portion of the supply water toward an external area not fluidically coupled to the cooling water at a flow rate between 1,000 and 12,000 gallons per minute.
14. The method of claim 13 , further comprising:
measuring a flow rate of the second portion of the supply water; and
introducing a makeup water into the cooling tower at a flow rate at least equivalent to the flow rate measured.
15. The method of claim 13 , wherein the ratio of the second portion of the supply water to metal produced in the industrial production facility is between 100 and 5000 gallons of supply water per ton of metal produced.
16. The method of claim 13 , wherein the ratio of the first portion of the supply water to metal produced in the industrial production facility is between 100 and 5000 gallons of supply water per ton of metal produced.
17. The method of claim 13 , further comprising directing a makeup water from a cooling water treatment system toward the cooling tower at a flow rate between 1,000 and 12,000 gallons per minute.
18. A system for treating cooling water in an iron production facility, the system comprising:
a cooling tower including a first cell and a second cell, each of the first and second cells including:
a housing positioned to receive a return water, and
a sump below the housing and configured to maintain a level of a supply water configured to be in direct contact with molten iron;
an inlet comprising an inlet line positioned to provide the return water to the cooling tower;
an outlet comprising an outlet line positioned to direct the supply water toward the iron production facility, wherein the inlet, the outlet, and the cooling tower form a loop;
a blowdown line fluidically coupled to the outlet and configured to direct a portion of the supply water away from the loop at a flow rate between 1,000 and 12,000 gallons per minute; and
a controller configured to monitor the loop,
wherein the cooling tower is configured to operate for at least 12 hours continuously.
19. The system of claim 1 , wherein the supply water within the loop is turned over between every 100 and 500 minutes.
20. The system of claim 1 , wherein a ratio of (i) the portion of the supply water directed away from the loop to (ii) metal produced in the industrial production facility is at least 100 gallons per ton of metal produced.