Method of inspecting gas supply system

Patent metadata

Field	Value
Publication number	US-10274972-B2
Application number	US-201615263490-A
Country	US
Kind code	B2
Filing date	Sep 13, 2016
Priority date	Sep 16, 2015
Publication date	Apr 30, 2019
Grant date	Apr 30, 2019

Abstract

A flow rate of a gas supplied into a processing vessel of a substrate processing apparatus is controlled according to a set flow rate of a first flow rate controller. The gas is also supplied into a second flow rate controller. When an output flow rate of the first flow rate controller is in a steady state, a first pressure measurement value of a first pressure gauge and a second pressure measurement value of a second pressure gauge of the second flow rate controller are obtained. A difference absolute value between the first pressure measurement value and a reference pressure value and a difference absolute value between the second pressure measurement value and a reference pressure value are calculated, and then, an average value of the difference absolute values is calculated. The difference absolute values and the average value are respectively compared with a first to third threshold value.

First claim

We claim:

1. A method of inspecting a gas supply system configured to supply a gas into a processing vessel of a substrate processing apparatus,
wherein the gas supply system comprises:
multiple first lines respectively connected to multiple gas sources;
multiple first valves respectively provided at the first lines;
multiple flow rate controllers respectively provided at downstream sides of the first lines and respectively connected to the first lines;
multiple second lines respectively provided at downstream sides of the flow rate controllers and respectively connected to the flow rate controllers;
multiple second valves respectively provided at the second lines;
a third line provided at downstream sides of the second lines and connected to the second lines; and
a third valve provided at the third line,
wherein the third line is connected to the processing vessel at a downstream side thereof, and
each of the flow rate controllers comprises an orifice, a fourth line extended at an upstream side of the orifice and connected to the first line, a fifth line extended at a downstream side of the orifice and connected to the second line, a control valve provided at the fourth line, a first pressure gauge configured to measure an internal pressure of the fourth line between the control valve and the orifice, and a second pressure gauge configured to measure an internal pressure of the fifth line, and
wherein the method comprises:
controlling a flow rate of the gas supplied into the processing vessel via a first flow rate controller among the flow rate controllers, the flow rate of the gas being controlled according to a set flow rate in the first flow rate controller;
opening, in a processing period during which the controlling of the flow rate of the gas is performed, one or more second valves, among the second valves, which are provided at downstream sides of one or more second flow rate controllers, among the flow rate controllers, which do not perform the controlling of the flow rate of the gas;
calculating one or more first difference absolute values and one or more second difference absolute values, each of the one or more first difference absolute values being a difference absolute value between a first reference steady pressure value and a first steady pressure value measured by the first pressure gauge of each of the one or more second flow rate controllers in a steady period during which an output flow rate of the first flow rate controller is in a steady state, each of the one or more second difference absolute values being a difference absolute value between a second reference steady pressure value and a second steady pressure value measured by the second pressure gauge of each of the one or more second flow rate controllers in the steady period, each of the first reference steady pressure value and the second reference steady pressure value being set prior to the processing period, and the first reference steady pressure value and the second reference steady pressure value being pressure measurement values measured by the first pressure gauge and the second pressure gauge of each of the one or more second flow rate controllers, respectively, when the output flow rate of the first flow rate controller, through which the flow rate of the gas supplied into the processing vessel is controlled according to the set flow rate, is in the steady state, wherein the first reference steady pressure value and the second reference steady pressure value are pressure measurement values obtained by the second flow rate controller in a steady state during a reference period prior to the processing period;
calculating an average value of the one or more first difference absolute values and the one or more second difference absolute values; and
determining whether the output flow rate of the first flow rate controller in the steady state during the processing period is changed from the output flow rate of the first flow rate controller in the steady state during the reference period by determining whether each of the one or more first difference absolute values is larger than a first threshold value, whether each of the one or more second difference absolute values is larger than a second threshold value, or whether the average value is large than a third threshold value.

2. The method of claim 1 ,
wherein the one or more second flow rate controllers are multiple second flow rate controllers, among the flow rate controllers, which do not perform the controlling of the flow rate of the gas in the processing period,
the one or more first difference absolute values are multiple first difference absolute values obtained by calculating the difference absolute value between the first reference steady pressure value and the first steady pressure value measured by the first pressure gauge of each of the multiple second flow rate controllers in the steady period, and the one or more second difference absolute values are multiple second difference absolute values obtained by calculating the difference absolute value between the second reference steady pressure value and the second steady pressure value measured by the second pressure gauge of each of the multiple second flow rate controller in the steady period,
the average value is an average value of the multiple first difference absolute values and the multiple second difference absolute values, and
in the determining, it is determined whether each of the multiple first difference absolute values is larger than the first threshold value, whether each of the multiple second difference absolute values is larger than the second threshold value, or whether the average value is larger than the third threshold value.

3. The method of claim 1 , further comprising:
calculating a sum value of pressure measurement values of the second pressure gauge of the first flow rate controller at multiple time points for a transient period prior to the steady period within the processing period; and
comparing the sum value with a preset reference value.

4. The method of claim 1 , further comprising:
calculating a sum value of pressure measurement values of the first pressure gauge of the one or more second flow rate controllers at multiple time points for a transient period prior to the steady period within the processing period; and
comparing the sum value with a preset reference value.

5. The method of claim 1 , further comprising:
determining whether a difference between a pressure measurement value of the first pressure gauge of the first flow rate controller in the processing period and a pressure measurement value of the second pressure gauge of the first flow rate controller in the processing period is equal to or smaller than a preset value.

6. The method of claim 1 , further comprising:
determining whether, in a state that the gas within the flow rate controllers is exhausted, a pressure measurement value of the first pressure gauge of each of the flow rate controllers is larger than a first preset value or a pressure measurement value of the second pressure gauge of each of the flow rate controllers is larger than a second preset value.

7. The method of claim 1 , further comprising:
determining whether, in a state that the gas within the flow rate controllers is exhausted, a difference absolute value between a moving average value of pressure measurement values measured by the first pressure gauge of each of the flow rate controllers and a moving average value of pressure measurement values measured by the second pressure gauge of each of the flow rate controllers within a preset time period is equal to or larger than a preset value.

8. The method of claim 1 , further comprising:
acquiring a first pressure mea

Assignees

• Tokyo Electron Ltd

Inventors

• Amikura Norihiko
• Miyoshi Risako

Classifications

• H10P95/00

  Generic processes or apparatus for manufacture or treatments not covered by the other groups of this subclass · CPC title

• G05B15/02

  electric · CPC title

• G05D7/0635 Primary

  by action on throttling means (G05D7/0688, G05D7/0694 take precedence) · CPC title

• G01F23/00

  Indicating or measuring liquid level or level of fluent solid material, e.g. indicating in terms of volume or indicating by means of an alarm · CPC title

• F16K31/004

  actuated by piezoelectric means · CPC title