Dilute chemical solution producing apparatus and dilute chemical solution producing method
US-10759678-B2 · Sep 1, 2020 · US
US11325851B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11325851-B2 |
| Application number | US-201716492947-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2017 |
| Priority date | Mar 30, 2017 |
| Publication date | May 10, 2022 |
| Grant date | May 10, 2022 |
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A diluted chemical liquid production apparatus has a structure that has a platinum group metal carrying resin column, a membrane-type deaeration apparatus and a gas dissolving membrane apparatus, which are sequentially provided in a supply line of ultrapure water; and has a pH adjuster injection device and an oxidation-reduction potential adjuster injection device, which are provided between the platinum group metal carrying resin column and the membrane-type deaeration apparatus. An inert gas source is connected to a gaseous phase side of the membrane-type deaeration apparatus, and an inert gas source is also connected to the gaseous phase side of the gas dissolving membrane apparatus; and a discharge line communicates with the gas dissolving membrane apparatus. A pH meter and an ORP meter are provided in the discharge line. Such a diluted chemical liquid production apparatus can control a pH and an oxidation-reduction potential.
Opening claim text (preview).
The invention claimed is: 1. A diluted chemical liquid production apparatus comprising: a platinum group metal carrying resin column and a membrane type deaeration apparatus, which are sequentially provided in an ultrapure water supply line; and a pH adjuster injection device for adding a pH adjuster into ultrapure water and an oxidation-reduction potential adjuster injection device for adding an oxidation-reduction potential adjuster, which are provided between the platinum group metal carrying resin column and the membrane type deaeration apparatus, and a diluted chemical liquid is obtained by adding the pH adjuster and the oxidation-reduction potential adjuster into ultrapure water; wherein the membrane type deaeration apparatus includes a liquid phase chamber for passing the diluted chemical liquid and a gaseous phase chamber for removing a gas dissolved in the diluted chemical liquid composed by a hydrophobic gas permeable membrane; wherein an inert gas is provided into the membrane type deaeration apparatus, and wherein a final diluted chemical liquid is obtained by passing ultrapure water through the platinum group metal carrying resin column, the pH adjuster injection device, the oxidation-reduction potential adjuster injection device and the membrane type deaeration apparatus. 2. The diluted chemical liquid production apparatus according to claim 1 , comprising a gas dissolving membrane apparatus for receiving the diluted chemical liquid deaerated by the membrane type deaeration apparatus. 3. The diluted chemical liquid production apparatus according to claim 1 , comprising pH measuring means and oxidation-reduction potential measuring means for measuring the diluted chemical liquid deaerated by the membrane type deaeration apparatus. 4. The diluted chemical liquid production apparatus according to claim 1 , wherein the pH adjuster is ammonia, and the oxidation-reduction potential adjuster is hydrogen peroxide.
Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor (separation of gases or vapours by diffusion B01D53/22) · CPC title
for obtaining ultra-pure water · CPC title
pH · CPC title
from semiconductor processing, e.g. waste water from polishing of wafers · CPC title
by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title
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