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Devices, systems, and methods employed in wet cleaning semiconductor devices are provided. In particular, systems that can deliver deionized water with the desired concentration of CO2 and methods of generating deionized water with a desired concentration of CO2 for use in wet cleaning of semiconduc

Devices, systems, and methods employed in wet cleaning semiconductor devices are provided. In particular, systems that can deliver deionized water with the desired concentration of CO2 and methods of generating deionized water with a desired concentration of CO2 for use in wet cleaning of semiconductor devices are provided.

대표청구항 ▼

1. A method for carbonation of deionized water comprising: supplying deionized water to a contactor;supplying carbon dioxide gas to the contactor;measuring, with at least one sensor, flow rate of the deionized water and temperature of the deionized water, wherein the at least one sensor is positione

1. A method for carbonation of deionized water comprising: supplying deionized water to a contactor;supplying carbon dioxide gas to the contactor;measuring, with at least one sensor, flow rate of the deionized water and temperature of the deionized water, wherein the at least one sensor is positioned at an inlet of the contactor or an outlet of the contactor;determining an amount of carbon dioxide gas to supply to the contactor such that a specific conductivity of carbonated deionized water is generated by the contactor in communication with the at least one sensor and the supply of carbon dioxide gas, wherein the determination is based on the measured flow rate and temperature;supplying the determined amount of carbon dioxide to the contactor via one or more flow restrictors and one or more valves that are in fluid communication with the supply of carbon dioxide gas and the contactor; andflowing the carbonated deionized water of a specific conductivity from the contactor. 2. The method of claim 1 further comprising varying the one or more valves between an open and a closed position such that an average amount of carbon dioxide gas that flows from the carbon dioxide gas source to the contactor is substantially equal to the determined amount of carbon dioxide gas supplied by the carbon dioxide gas source. 3. The method of claim 1 further comprising purging an amount of the carbon dioxide gas through an outlet of the contactor. 4. The method of claim 3 further comprising determining the amount of carbon dioxide gas to purge such that a specific conductivity of the carbonated deionized water is generated in the contactor. 5. The method of claim 3 further comprising at least one flow restrictor in fluid communication with the outlet of the contactor and a drain for controlling the amount and flow rate of carbon dioxide gas purged from the contactor. 6. The method of claim 3 further comprising at least one flow orifice in fluid communication with the outlet of the contactor and a drain for controlling the amount and flow rate of carbon dioxide gas purged from the contactor. 7. The method of claim 1 further comprising setting a pressure of carbon dioxide gas at the at least one inlet. 8. The method of claim 1 further comprising mixing deionized water provided by the deionized water source and carbon dioxide provided by the carbon dioxide source prior to entering the contactor. 9. The method of claim 1 further comprising: measuring flow rate, with a first sensor, of the deionized water at an inlet of the contactor; andmeasuring temperature, with a second sensor, of the deionized water at an outlet of the contactor. 10. The method of claim 1 further comprising: measuring temperature, with a first sensor, of the deionized water at an inlet of the contactor; andmeasuring flow rate, with a second sensor, of the deionized water at an outlet of the contactor.