IPC분류정보
국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
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출원번호 |
US-0058327
(2005-02-15)
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등록번호 |
US-7435447
(2008-10-14)
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발명자
/ 주소 |
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출원인 / 주소 |
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대리인 / 주소 |
Wood, Herron & Evans, L.L.P.
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인용정보 |
피인용 횟수 :
3 인용 특허 :
200 |
초록
▼
In a high pressure processing system configured to treat a substrate, a flow measurement device is utilized to determine a flow condition in the high pressure processing system. The flow measurement device can, for example, comprise a turbidity meter. The flow parameter can, for example, include a v
In a high pressure processing system configured to treat a substrate, a flow measurement device is utilized to determine a flow condition in the high pressure processing system. The flow measurement device can, for example, comprise a turbidity meter. The flow parameter can, for example, include a volume flow rate or a time to achieve mixing of a process chemistry within a high pressure fluid used to treat the substrate.
대표청구항
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What is claimed is: 1. A method of treating a substrate comprising: placing said substrate in a high pressure processing chamber of a high pressure processing system onto a platen configured to support said substrate; forming a supercritical fluid from a fluid by adjusting a pressure of said fluid
What is claimed is: 1. A method of treating a substrate comprising: placing said substrate in a high pressure processing chamber of a high pressure processing system onto a platen configured to support said substrate; forming a supercritical fluid from a fluid by adjusting a pressure of said fluid above the critical pressure of said fluid, and adjusting a temperature of said fluid above the critical temperature of said fluid; introducing said supercritical fluid to said high pressure processing chamber; introducing a process chemistry to said supercritical fluid; flowing said supercritical fluid and said process chemistry over said substrate; measuring a flow condition that varies with the concentration of said process chemistry in said supercritical fluid flowing past a flow condition measurement device; determining a flow rate of said supercritical fluid and process chemistry through said system from a variation of said measured flow condition; and recirculating said supercritical fluid through said high pressure processing chamber; said determining said flow rate comprising determining a volume of said supercritical fluid circulating through said high pressure processing system, and dividing said volume by a difference in time between a first variation in a signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a first time and a second variation in said signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a second time. 2. The method of claim 1, further comprising: adjusting said flow rate of said supercritical fluid and said process chemistry according to a difference between said measured value of said flow rate and a target value of said flow rate. 3. The method of claim 1, further comprising: adjusting said flow rate of said supercritical fluid in response to the actual flow rate determination. 4. The method of claim 1, further comprising: determining the homogeneity of said supercritical fluid as a result of the flow rate determination; and timing the said flowing of said supercritical fluid and said process chemistry over said substrate in response to the homogeneity determination. 5. The method of claim 1, wherein said flow condition measurement device is selected from a group which consists of at least one coriolis meter, at least one turbidity meter, or a combination thereof. 6. The method of claim 1, wherein said measuring a flow condition further comprises; measuring the homogeneity of said process chemistry in said supercritical fluid, wherein said supercritical fluid is flowing through a recirculation loop bypassing said high pressure processing chamber prior to flowing said supercritical fluid and said process chemistry over said substrate. 7. The method of claim 1, wherein said determining said flow rate further comprises: using two or more turbidity meters, whereby the distance between said turbidity meters is known and the time difference between a first time associated with the passing of a flow disturbance by a first turbidity meter and a second time associated with the passing of said flow disturbance by a second turbidity meter is utilized to determine said flow rate. 8. The method of claim 1, wherein the volume ratio of said process chemistry to said supercritical fluid is within the range of from about 1 to 15 v/v %. 9. The method of claim 1, wherein said introducing a process chemistry further comprises: selecting said process chemistry from the group consisting of chemicals used for solvents, co-solvents, surfactants, etchants, acids, bases, chelators, oxidizers, film-forming precursors, or reducing agents, or any combination thereof. 10. The method of claim 1, wherein said substrate consists of semiconductor material, metallic material, dielectric material, ceramic material, or polymer material, or a combination of two or more thereof. 11. The method of claim 10, wherein said forming a supercritical fluid is accomplished by selecting said fluid from the group consisting of carbon dioxide, oxygen, argon, krypton, xenon, ammonia, methane, methanol, dimethyl ketone, hydrogen, water, and sulfur hexafluoride. 12. The method of claim 11, wherein said introducing a process chemistry further comprises: selecting said process chemistry from the group consisting of chemicals used for solvents, co-solvents, surfactants, etchants, acids, bases, chelators, oxidizers, film-forming precursors, or reducing agents, or any combination thereof. 13. The method of claim 12, wherein the volume ratio of said process chemistry to said supercritical fluid is within the range of from about 1 to 15 v/v %. 14. The method of claim 13, wherein said measuring a flow condition further comprises; measuring the homogeneity of said process chemistry in said supercritical fluid, wherein said process chemistry and said supercritical fluid are flowing through a recirculation loop bypassing said high pressure processing chamber prior to flowing said process chemistry in said supercritical fluid over said substrate. 15. A method of treating a substrate comprising: placing said substrate in a high pressure processing chamber of a high pressure processing system onto a platen configured to support said substrate; forming a supercritical fluid from a fluid by adjusting a pressure of said fluid above the critical pressure of said fluid, and adjusting a temperature of said fluid above the critical temperature of said fluid; introducing said supercritical fluid to said high pressure processing chamber; introducing a process chemistry to said supercritical fluid; flowing said supercritical fluid and said process chemistry over said substrate; measuring a flow condition that varies with the concentration of said process chemistry in said supercritical fluid flowing past a flow condition measurement device; determining a flow rate of said supercritical fluid and process chemistry through said system from a variation of said measured flow condition; and said measuring a flow condition further comprising measuring the homogeneity of said process chemistry in said supercritical fluid, wherein said supercritical fluid is flowing through a recirculation loop bypassing said high pressure processing chamber prior to flowing said supercritical fluid and said process chemistry over said substrate; said substrate consists of semiconductor material, metallic material, dielectric material, ceramic material, or polymer material, or a combination of two or more thereof; said forming a supercritical fluid being accomplished by selecting said fluid from the group consisting of carbon dioxide, oxygen, argon, krypton, xenon, ammonia, methane, methanol, dimethyl ketone, hydrogen, water, and sulfur hexafluoride; said introducing a process chemistry further comprising selecting said process chemistry from the group consisting of chemicals used for solvents, co-solvents, surfactants, etchants, acids, bases, chelators, oxidizers, film-forming precursors, or reducing agents, or any combination thereof; the volume ratio of said process chemistry to said supercritical fluid being within the range and including about 1 to 15 v/v %; said measuring a flow condition further comprising measuring the homogeneity of said process chemistry in said supercritical fluid, wherein said process chemistry and said supercritical fluid are flowing through a recirculation loop bypassing said high pressure processing chamber prior to flowing said process chemistry in said supercritical fluid over said substrate; said measuring said homogeneity of said process chemistry in said supercritical fluid further comprising determining a mixing time of said process chemistry in said supercritical fluid through said recirculation loop by observing when a difference in signal subsides to a negligible amount, wherein said difference in signal is between a first variation in a signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a first time and a subsequent variation in said signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a subsequent time. 16. A method of treating a substrate comprising: placing said substrate in a high pressure processing chamber of a high pressure processing system onto a platen configured to support said substrate; forming a supercritical fluid from a fluid by adjusting a pressure of said fluid above the critical pressure of said fluid, and adjusting a temperature of said fluid above the critical temperature of said fluid; introducing said supercritical fluid to said high pressure processing chamber; introducing a process chemistry to said supercritical fluid; flowing said supercritical fluid and said process chemistry over said substrate; measuring a flow condition that varies with the concentration of said process chemistry in said supercritical fluid flowing past a flow condition measurement device; determining a flow rate of said supercritical fluid and process chemistry through said system from a variation of said measured flow condition; and said measuring a flow condition further comprising measuring the homogeneity of said process chemistry in said supercritical fluid, wherein said supercritical fluid is flowing through a recirculation loop bypassing said high pressure processing chamber prior to flowing said supercritical fluid and said process chemistry over said substrate; said measuring said homogeneity of said process chemistry in said supercritical fluid comprising: determining a volume of said supercritical fluid circulating through said recirculation loop, and dividing said volume by a difference in time between a first variation in a signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a first time and a second variation in said signal from said flow condition measurement device as said process chemistry in said supercritical fluid passes said flow condition measurement device a second time.
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