System and method to sustainable integrated wastewater treatment and air-cooling in a steelmaking plant

Patent metadata

Field	Value
Publication number	US-12195361-B2
Application number	US-202318112140-A
Country	US
Kind code	B2
Filing date	Feb 21, 2023
Priority date	Feb 21, 2023
Publication date	Jan 14, 2025
Grant date	Jan 14, 2025

Abstract

Some implementations provide an integrated system that includes: a wastewater treatment system configured to process wastewater released by one or more furnaces at a steelmaking plant, and generates reused wastewater using the wastewater; a heat recovery apparatus configured to utilize exhaust gas from the one or more furnaces at the steelmaking plant, and heat the reused wastewater generated by the wastewater treatment system above a threshold temperature; and a generator configured to receive, through a water inlet, the reused wastewater heated above the threshold temperature; and an absorption system arranged in circulation with the generator, and wherein the reused water is supplied above a threshold amount such that the generator drives the absorption system and produces cooled air inside the steelmaking plant.

First claim

What is claimed is:

1. A system comprising:
a wastewater treatment system configured to process wastewater released by one or more furnaces at a steelmaking plant, and generate reused wastewater;
a heat recovery apparatus coupled to the wastewater treatment system and a freshwater tank through at least one valve to receive a mixture of reused wastewater and fresh water, wherein the heat recovery apparatus is configured to heat the mixture of reused wastewater and fresh water, using exhaust gas from the one or more furnaces at the steelmaking plant, above a threshold temperature; and
a generator coupled to the heat recovery apparatus and configured to receive, through a water inlet of the generator, the mixture of reused wastewater and fresh water heated above the threshold temperature; and
an absorption system in circulation with the generator, wherein the mixture of reused wastewater and fresh water is supplied above a threshold amount such that the generator drives the absorption system and produces cooled air inside the steelmaking plant.

2. The system of claim 1 , further comprising:
a control system comprising one or more computer processors and configured to assert control, using the one or more computer processors, over the wastewater treatment system, the heat recovery apparatus, the generator, and the absorption system, wherein the control system is arranged in communication with the wastewater treatment system, the heat recovery apparatus, the generator, and the absorption system.

3. The system of claim 2 , wherein the control system is further configured to:
in response to receiving information that the mixture of reused wastewater and fresh water does not reach the threshold amount, use the one or more computer processors to automatically control an emergency valve such that additional fresh water is provided from the freshwater tank to the generator.

4. The system of claim 2 , wherein the absorption system comprises: a lithium bromide (LiBr) absorption system.

5. The system of claim 2 , wherein the absorption system comprises:
a condenser coupled to the generator;
an evaporator coupled to the condenser through a first expansion valve; and
an absorber coupled to the evaporator, wherein the absorber is further coupled to the generator through a pump and a second expansion valve.

6. The system of claim 2 , wherein the control system is configured to operate the generator in tandem with the wastewater treatment system such that the steelmaking plant is cooled exclusively by cooled air from the absorption system.

7. The system of claim 1 , wherein the one or more furnaces comprise at least one electric arc furnace (EAF).

8. The system of claim 1 , wherein the wastewater treatment system operates on grid power.

9. The system of claim 1 , wherein the wastewater treatment system is configured to apply a physical separation, or a chemical separation method, to wastewater from the furnaces at the steelmaking plant.

10. The system of claim 1 , wherein the wastewater treatment system is configured to process more than 200,000 m 3 /year of wastewater.

11. The system of claim 10 , wherein the steelmaking plant has a liquid steel production capacity of between 0.4 and 0.6 million ton/year.

12. A computer-implemented method comprising:
generating reused wastewater using a wastewater treatment system that processes wastewater released by one or more furnaces at a steelmaking plant;
heating a mixture of the reused wastewater provided by the wastewater treatment system and fresh water provided by a freshwater tank, wherein said heating utilizes exhaust gas from the one or more furnaces at the steelmaking plant, and wherein said heating causes the mixture of reused wastewater and fresh water to be exceed a threshold temperature; and
supplying, using a water inlet, the mixture of reused wastewater and fresh water heated above the threshold temperature to a generator, wherein the mixture of reused wastewater and fresh water is supplied above a threshold amount such that the generator drives an absorption system arranged in circulation with the generator and configured to produce cooled air inside the steelmaking plant.

13. The computer-implemented method of claim 12 , further comprising:
asserting control over said generating, said heating and said supplying, using a control system that comprises at least one computer processor.

14. The computer-implemented method of claim 13 , wherein, when the mixture of reused wastewater and fresh water does not reach the threshold amount, opening an emergency valve such that additional fresh water is provided from the freshwater tank.

15. The computer-implemented method of claim 13 , further comprising:
asserting control over the absorption system that comprises a lithium bromide (LiBr) absorption system.

16. The computer-implemented method of claim 15 , wherein asserting control comprises asserting control over a condenser coupled to the generator, an evaporator coupled to the condenser through a first expansion valve, and an absorber coupled to the evaporator, wherein the absorber is further coupled to the generator through a pump and a second expansion valve.

17. The computer-implemented method of claim 12 , wherein the one or more furnaces comprise at least one electric arc furnace (EAF).

18. The computer-implemented method of claim 12 , further comprising:
operating the wastewater treatment system using grid power.

19. The computer-implemented method of claim 12 , wherein operating the wastewater treatment system comprises: applying at least one of: a physical separation, or a chemical separation method, to wastewater from the furnaces at the steelmaking plant.

20. The computer-implemented method of claim 12 , further comprising:
operating the generator in tandem with the wastewater treatment system such that the steelmaking plant is cooled exclusively by cooled air from the absorption system.

Assignees

• Saudi Arabian Oil Co

Inventors

• Almutairi Faisal B
• Al-Ugla Ali Abdulaziz

Classifications

• F27D17/304

  specially adapted for electric arc furnaces · CPC title

• C02F1/048

  Purification of waste water by evaporation · CPC title

• C21C5/5264

  Manufacture of alloyed steels including ferro-alloys · CPC title

• C21C2100/06

  Energy from waste gas used in other processes · CPC title

• C21C2300/06

  Modeling of the process, e.g. for control purposes; CII · CPC title