Pressure-less ozonated Di-water (DIO
The invention provides, in one aspect, a system for recirculating ozonated liquid. The system includes a contactor including at least two inlets and at least two outlets. The contactor is in fluid communication with a first liquid source at a first contactor inlet and a second liquid source at a second contactor inlet, and the second contactor inlet receives gas that purges at least a portion of gas from liquid received at the first contactor inlet. The purged gas exits the contactor at a first contactor outlet. The contactor is in fluid communication with the second liquid source at a second contactor outlet, and the contactor drains at least a portion of the liquid in the contactor, the drained liquid exiting the contactor at the second contactor outlet. The contactor includes a third inlet in fluid communication with the first liquid source, the third inlet allowing the first liquid source to release liquid at an ambient pressure.
1. A system for recirculating ozonated liquid, comprising:
a contactor including at least two inlets and at least two outlets, the contactor being in fluid communication with a first liquid source at a first contactor inlet and a second liquid source at a second contactor inlet, the second contactor inlet receiving gas that purges at least a portion of gas from liquid received at the first contactor inlet, the purged gas exiting the contactor at a first contactor outlet,
wherein the contactor is in fluid communication with the second liquid source at a second contactor outlet, the contactor draining at least a portion of the liquid in the contactor, the drained liquid exiting the contactor at the second contactor outlet, and
wherein the contactor includes a third inlet in fluid communication with the first liquid source, the third inlet allowing the first liquid source to release liquid at an ambient pressure.
2. The system of claim 1 , wherein at least a portion of the liquid received at the first contactor inlet comprises at least a portion of the liquid drained from the contactor via the second contactor outlet.
3. The system of claim 1 , wherein the contactor includes a fourth inlet in fluid communication with a third a liquid source, the fourth inlet receiving fresh liquid from the third liquid source that replaces at least a portion of the liquid drained from the contactor.
4. The system of claim 1 , wherein the contactor comprises any of a packed column, plate column, or bubble column.
5. The system of claim 1 , further comprising a first pump in fluid communication with the contactor via a) at least one inlet of the first pump being in fluid communication with the second outlet of the contactor, and b) an outlet of the first pump being in fluid communication with the second liquid source.
6. The system of claim 5 , wherein the outlet of the first pump is in fluid communication with the contactor via a fourth inlet of the contactor.
7. The system of claim 5 , where in the first pump comprises a centrifugal pump.
8. The system of claim 1 , further comprising a destruct component that includes at least an inlet, the inlet of the destruct component in fluid communication with the first contactor outlet.
9. The system of claim 8 , wherein the inlet of the destruct component receives at least a portion of the gas purged by the contactor.
10. The system of claim 9 , wherein the gas received at the first inlet of the destruct component is heated or diluted with CDA or other inert gas.
11. The system of claim 9 , wherein an outlet of the destruct component exhausts at least a portion of the purged gas received at the inlet of the destruct component.
12. The system of claim 10 , wherein a gas flow at the outlet of the destruct component is measured and the information is used for system control.
13. The system of claim 11 , wherein the destruct component uses a catalyst to convert the received gas into oxygen and exhausts the oxygen via the outlet of the destruct component.
14. The system of claim 13 , wherein the catalyst comprises any of (i) manganese-oxide based product or (ii) a carbon-based product.
15. The system of claim 1 , wherein any of the liquid (i) received at the first inlet of the contactor or (ii) drained from the second outlet of the contactor, comprises ozonated deionized water (DIO 3 ).
16. The system of claim 1 , wherein the gas received at the first inlet of the contactor comprises (i) O 3 , (ii) O 2 , (iii) CO 2 , (iv) N 2 , (iv) Clean Dry Air (CDA), (v) inert gas, (vi) doping gas, (vii) off-gas, (viii) off-gas from the second liquid source, or any combination thereof.
17. The system of claim 1 , wherein the portion of gas purged from the liquid comprises (i) O 3 , (ii) O 2 (iii) CO 2 , or any combination thereof.
18. The system of claim 17 , wherein the gas received at the first inlet of the contactor is the off-gas from the second liquid source.
19. The system of claim 1 , wherein the first liquid source comprises a tool used in a semiconductor manufacturing process.
20. The system of claim 1 , wherein a temperature of the liquid is measured and a temperature of the liquid is controlled via a heat exchanger or by liquid discarding.
21. The system of claim 1 , wherein the second liquid source comprises a DIO 3 water delivery system.
22. The system of claim 5 , further comprising a second pump being in fluid communication with any of (i) the first outlet of the first pump, or (ii) a second outlet of the first pump.
23. The system of claim 22 , wherein the second pump comprises a jet pump.