Abstract:
A method for producing ozone gas-dissolved water includes a process in which a mixed gas of an ozone gas and an oxygen gas and degassed water are supplied to an ozone-dissolving section and the mixed gas is dissolved in the degassed water. The amount of the mixed gas supplied to the ozone-dissolving section is controlled such that the sum of the dissolved oxygen gas concentration of the degassed water and the increment of the dissolved oxygen gas concentration calculated from the amount of the oxygen gas in the mixed gas and the amount of the degassed water on the assumption that ozone in the mixed gas entirely decomposes into oxygen is less than or equal to the saturated solubility of the oxygen gas under conditions using the obtained ozone gas-dissolved water.
Abstract:
A dilute chemical solution producing apparatus includes, in a supply line of ultrapure water, a platinum group metal carrying resin column, a membrane-type deaeration apparatus, and a gas dissolving membrane apparatus, and a washing chemical solution injection apparatus is provided between the platinum group metal carrying resin column and the membrane-type deaeration apparatus. An inert gas source is connected to a gas phase side of the membrane-type deaeration apparatus, and an inert gas source is also connected to a gas phase side of the gas dissolving membrane apparatus. A discharge line communicates with the gas dissolving membrane apparatus. With such a dilute chemical solution producing apparatus, a dilute chemical solution with both dissolved oxygen and dissolved hydrogen peroxide being removed can be safely produced and supplied in a washing step for semiconductor washing.
Abstract:
A method for treating drainage containing hydrogen peroxide that has been used for sterilizing and washing an inside of a water treatment system or washing and surface finishing of electronic components includes passing the drainage through the hydrogen peroxide decomposition reactor, injecting effluent water from the hydrogen peroxide decomposition reactor into a side part of the tubular container of the gas-liquid separator, and contacting the drainage with the hydrogen peroxide decomposition catalyst to decompose the hydrogen peroxide in the drainage into oxygen and water, thereby yielding the treated water.
Abstract:
A solution having a predetermined concentration is stably supplied to a use point, at which the amount of use of the solution changes, by only modifying currently-used equipment at a low cost and in a space-saving manner. In order to supply a solution containing a solute at a predetermined concentration from a preparation portion of the solution to a use point through a supply pipe, a retention portion that has no gas-liquid interface and at which the solution is retained is provided at an intermediate portion of the supply pipe. Even when the amount of use of the solution at the use point changes, the change is absorbed by the retention portion, whereby a solution having a predetermined concentration can be stably supplied to the use point. Such a retention portion is advantageous in terms of space saving since the retention portion can be formed by using, for example, a long pipe portion or a large-diameter portion of a pipe having no gas-liquid interface. Such a retention portion can be installed in existing equipment at a low cost by only slightly modifying an intermediate portion of a supply pipe.