Flow rate controller, gas supply system, and flow rate control method
US-2021111004-A1 · Apr 15, 2021 · US
US11644121B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11644121-B2 |
| Application number | US-202117189804-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 2, 2021 |
| Priority date | Mar 24, 2020 |
| Publication date | May 9, 2023 |
| Grant date | May 9, 2023 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A gas inspection method includes: inputting a signal for opening a secondary valve; measuring, by a secondary pressure gauge, a pressure P on a downstream side of an orifice of a flow rate controller at a time point when a period t elapses from the input of the signal for opening the secondary valve; measuring, by the secondary pressure gauge, a standard deviation σ of the pressure P on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses from the input of the signal for opening the secondary valve; and determining whether or not an open degree of the secondary valve is normal by comparing the pressure P and the standard deviation σ of the pressure P with a threshold value P0 of the pressure and a threshold value σ0 of the standard deviation of the pressure.
Opening claim text (preview).
What is claimed is: 1. A gas inspection method of inspecting a gas supply configured to supply a gas into a chamber, wherein the gas supply includes a pipe configured to connect a gas source and the chamber to each other, a flow rate controller provided in the pipe, a primary valve provided on an upstream side of the flow rate controller, and a secondary valve provided on a downstream side of the flow rate controller, and wherein the flow rate controller includes an orifice, a primary pressure gauge provided on an upstream side of the orifice, and a secondary pressure gauge provided on a downstream side of the orifice, the method comprising: (a) setting, in the flow rate controller, a threshold value P 0 of a pressure on the downstream side of the orifice of the flow rate controller at a time point when a period t elapses from an input of a signal for opening the secondary valve, and a threshold value σ 0 of a standard deviation of the pressure; (b) inputting the signal for opening the secondary valve; (c) measuring, by the secondary pressure gauge, a pressure P on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses from the input of the signal for opening the secondary valve; (d) measuring, by the secondary pressure gauge, a standard deviation σ of the pressure P on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses from the input of the signal for opening the secondary valve; and (e) determining whether or not an open degree of the secondary valve is normal by comparing the pressure P measured in (c) and the standard deviation σ of the pressure P measured in (d) with the threshold value P 0 of the pressure and the threshold value σ 0 of the standard deviation of the pressure, which are set in (a), respectively. 2. The gas inspection method of claim 1 , wherein the threshold value P 0 of the pressure, which is set in (a), on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses after the input of the signal for opening the secondary valve is 10 kPa to 30 kPa, and the threshold value σ 0 of the standard deviation of the pressure is 1 kPa to 5 kPa. 3. The gas inspection method of claim 1 , wherein the period tin (a), (b), and (c) is five seconds to ten seconds. 4. The gas inspection method of claim 1 , wherein (a) includes setting the threshold value P 0 of the pressure and the threshold value σ 0 of the standard deviation of the pressure from the pressure P measured by the secondary pressure gauge when the secondary valve is normally opened and a standard deviation of the pressure P measured by the secondary pressure gauge when the secondary valve is normally opened, respectively. 5. The gas inspection method of claim 1 , further comprising: (i) when the pressure P measured in (c) is determined in (e) to be equal to or less than the threshold value P 0 of the pressure set in (a) and the standard deviation σ of the pressure P measured in (d) is determined in (e) to be equal to or less than the threshold value σ 0 of the standard deviation of the pressure set in (a), determining that an operation of opening the secondary valve is normal and continuing processing a substrate. 6. A substrate processing method, comprising: the method of inspecting the gas supply according to claim 1 , wherein a substrate is processed using the gas supplied from the gas supply. 7. The gas inspection method of claim 1 , wherein (a) includes: (f) measuring, a plurality of times by the secondary pressure gauge, the pressure P when the secondary valve is in a normally opened state under specific processing conditions and a standard deviation of the pressure P when the secondary valve is in the normally opened state under the specific processing conditions; and (g) setting the threshold value P 0 of the pressure and the threshold value σ 0 of the standard deviation of the pressure based on the pressures and standard deviations measured in (f), respectively. 8. The gas inspection method of claim 7 , wherein (g) includes setting the threshold value P 0 of the pressure and the threshold value σ 0 of the standard deviation of the pressure to be values obtained by multiplying a maximum value among the pressures measured in (f) by a first coefficient and multiplying a maximum value among the standard deviations measured in (f) by a second coefficient, respectively. 9. The gas inspection method of claim 8 , wherein each of the first coefficient and the second coefficient falls within a range of 1 to 8. 10. A system for processing a substrate using a gas, the system comprising: a chamber including a gas supply port and a gas exhaust port; a gas supply configured to supply the gas to the chamber; and a controller, wherein the gas supply includes a pipe configured to connect a gas source and the chamber to each other, a flow rate controller provided in the pipe, a primary valve provided on an upstream side of the flow rate controller, and a secondary valve provided on a downstream side of the flow rate controller, wherein the flow rate controller includes an orifice, a primary pressure gauge provided on an upstream side of the orifice, and a secondary pressure gauge provided on a downstream side of the orifice, and wherein the controller is configured to control the system to execute a processing including processes of: (a) setting, in the flow rate controller, a threshold value P 0 of a pressure on the downstream side of the orifice of the flow rate controller at a time point when a period t elapses from an input of a signal for opening the secondary valve, and a threshold value σ 0 of a standard deviation of the pressure; (b) inputting the signal for opening the secondary valve; (c) measuring, by the secondary pressure gauge a pressure P on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses from the input of the signal for opening the secondary valve; (d) measuring, by the secondary pressure gauge a standard deviation σ of the pressure P on the downstream side of the orifice of the flow rate controller at the time point when the period t elapses from the input of the signal for opening the secondary valve; and (e) determining whether or not an open degree of the secondary valve is normal by comparing the pressure P measured in (c) and the standard deviation σ of the pressure P measured in (d) with the threshold value P 0 of the pressure and the threshold value σ 0 of the standard deviation of the pressure, which are set in (a).
of Group IV materials · CPC title
Apparatus for fluid treatment (H10P72/0441, H10P72/0448 take precedence) · CPC title
Process monitoring, e.g. flow or thickness monitoring · CPC title
characterised by the use of electric means {(G05D7/005 takes precedence)} · CPC title
by measuring pressure or differential pressure · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.