Method and apparatus for creating ozonated process solutions having high ozone concentration
A method and system for creating an ozonated process solution, such as ozonated deionized water, having high ozone concentration. The system comprises, a static mixer coupled to a recirculation loop of an auxiliary tank. The system and method are designed so that during the initial feed of process liquid and ozone gas to the system, the process liquid and ozone gas pass through the static mixer prior to ever reaching the auxiliary. The static mixer mixes the ozone gas into the process liquid to form the ozonated process solution. Thus, the auxiliary tank is initially filled with an ozonated process solution. The ozonated process solution can be recirculated from the auxiliary tank and back through the static mixer while additional ozone gas is dissolved therein. This recirculation can be performed until a desired concentration of ozone is detected in the ozonated process solution.
1 . A system for creating an ozonated process solution comprising:
an auxiliary tank having an inlet and an outlet;
a recirculation line fluidly connecting the inlet and the outlet, and having a pump for circulating fluids from the outlet to the inlet;
a static mixer operably and fluidly connected to the recirculation line;
a process liquid supply line fluidly connected to the recirculation line at or upstream of the static mixer; and
an ozone gas supply line fluidly connected to the recirculation system at or upstream of the static mixer.
2 . The system of claim 1 further comprising a controller adapted to activate the process liquid supply line and the ozone gas liquid supply line upon receiving a system activation signal so that the auxiliary tank is initially supplied with an ozonated process solution created by the static mixer.
3 . The system of claim 2 wherein the controller is further adapted to stop supply of process liquid to the recirculation line upon a desired volume of ozonated process liquid being supplied to the auxiliary tank, the controller further adapted to activate the pump to circulate the ozonated process solution through the recirculation line where additional ozone gas is added via the static mixer.
4 . The system of claim 1 further comprising a sensor for measuring ozone concentration, the sensor coupled to the recirculation line.
5 . The system of claim 1 further comprising a dispense line for supplying ozonated process solution from the auxiliary tank to a process chamber.
6 . The system of claim 5 further comprising valve means for switching flow of the ozonated process solution from through the recirculation line to the dispense line upon a desired concentration of ozone being detected in the ozonated process solution.
7 . The system of claim 6 further comprising a process chamber supporting at least one semiconductor wafer to be subjected to the ozonated process liquid.
8 . The system of claim 1 wherein the auxiliary tank is under pressure.
9 . The system of claim 8 wherein the auxiliary tank comprises a pressurized gaseous atmosphere.
10 . The system of claim 9 wherein the gaseous atmosphere consists essentially of nitrogen gas.
11 . The system of claim 1 further comprising a liquid level sensor positioned in the auxiliary tank for measuring the amount of ozonated process solution in the auxiliary tank.
12 . The system of claim 1 wherein the process liquid is DI water, the system further comprising a DI water reservoir.
13 . The system of claim 1 further comprising a source of ozone.
14 . The system of claim 13 wherein the source of ozone is an ozone generator.
15 . The system of claim 14 further comprising a source of carbon dioxide fluidly connect to the ozone generator.
16 . The system of claim 1 wherein the static mixer comprises a plurality of baffles adapted to cause turbulent fluid flow within the static mixer.
17 . A method for creating an ozonated process solution having a desired ozone concentration comprising:
introducing a process liquid and an ozone gas to a static mixer prior to entering an auxiliary tank;
mixing the process liquid and the ozone gas in the static mixer to create an ozonated process solution;
providing the ozonated process solution to the auxiliary tank;
recirculating ozonated process solution from the auxiliary tank, through the static mixer, and back into the auxiliary tank while continuing to introduce the ozone gas in the static mixer;
measuring concentration of ozone gas in the ozonated process solution leaving the auxiliary tank during the recirculation step; and
continuing the recirculating step until the measured concentration of ozone gas in the ozonated process solution is equal to the desired concentration.
18 . The method of claim 17 further comprising:
measuring the amount of ozonated process solution in the auxiliary tank; and
upon a desired amount of ozonated process solution being in the auxiliary tank, ceasing the introduction of the process liquid.
19 . The method of claim 17 wherein the process liquid is DI water.
20 . The method of claim 17 further comprising:
measuring the amount of ozonated process solution provided to the auxiliary tank during the providing step; and
upon a desired amount of ozonated process solution being in the auxiliary tank, ceasing the introduction of the process liquid;
wherein the recirculating step is not undertaken until the desired amount of ozonated process solution is in the auxiliary tank.
21 . The method of claim 17 further comprising:
creating the ozone gas prior to the introduction with an ozone generator.
22 . The method of claim 17 wherein the auxiliary tank is under pressure.
23 . The method of claim 22 further comprising providing a pressurized gaseous atmosphere in the auxiliary tank.
24 . The method of claim 23 wherein the gaseous atmosphere consists essentially of nitrogen gas.
25 . The method of claim 17 further comprising the step of introducing carbon dioxide gas with the ozone gas.