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US3650042A - Gas barrier for interconnecting and isolating two atmospheres - Google Patents

Gas barrier for interconnecting and isolating two atmospheres
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Publication number
US3650042A
US3650042AUS825777AUS3650042DAUS3650042AUS 3650042 AUS3650042 AUS 3650042AUS 825777 AUS825777 AUS 825777AUS 3650042D AUS3650042D AUS 3650042DAUS 3650042 AUS3650042 AUS 3650042A
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pressure
compartments
tier
reactive
inlet
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US825777A
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Frank E Boerger
William H White
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International Business Machines Corp
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International Business Machines Corp
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Abstract

A transition or isolation zone for accommodating continuous free flow of a tier of articles between two distinct and isolated atmospheres. The transition zone includes a series of alternate inlet and outlet compartments for a non-reactive gas wherein the compartments contain inlet and outlet openings interconnecting with each other and the indicated atmospheres. The cross sections of the openings are complementary to the cross section of the tier of articles to provide a restricted orifice-size clearance therebetween, whereby the orifice phenomena can be employed by correlation of pressures to control the flow of gas and conversely to substantially completely isolate the indicated atmospheres without any measurable cross-migration therebetween.

Description

United States Patent Boerger et al. 5] Mar. 21, 1972 54] GAS BARRIER FOR 2,963,001 12/1960 Alexander ..34 242 x INTERCONNECTING AND ISOLATING 3,067,602 l2/ 1962 Brunt ..68/5 E woS E S 1 3,349,578 10/1967 Greer ..34/242 X [72] Inventors: Frank E. Boerger; William H. White, both Primary Examiner-Edward J. Michael of Poughkeepsie, NY. Attorney-Hanifin and Jancin and Henry Powers [73] Assignee: International Business Machines Corpora- ABSTRACT tion, Armonk, NY.
A transition or isolation zone for accommodating continuous free flow of a tier of articles between two distinct and isolated atmospheres. The transition zone includes a series of alternate inlet and outlet compartments for a non-reactive gas wherein the compartments contain inlet and outlet openings interconnecting with each other and the indicated atmospheres. The cross sections of the openings are complementary to the cross section of the tier of articles to provide a restricted orifice-size clearance therebetween, whereby the orifice phenomena can be employed by correlation of pressures to control the flow of gas and conversely to substantially completely isolate the indicated atmospheres without any measurable cross-migration therebetween.
38 Claims, 71 Drawing Figures SHEET 01UF46 PATENTEUHARZI I972 INVENTORS FRANK E. BOERGER WILLIAM H. mm
ATTORNEY FIG.2
PATENTEB MAR 2!i972 SHEET 02 0F 46 SHEET 030F 46 PAIENTEDHARZIm2 PAIENTEB MAR 21 m2 SHEET on or 46 PAIENIEUMAR21 m2 SHEET 080F 16 PATENTEBMAR21 I972 SHEET 07UF 46 PATENTEDIARZ'I I972 SHEET 080F 16 m. wE
PATENTEnMARm I972 SHEET 1UUF46 PAIENTEDMAR21 I972 SHEET 110F416 s l. :T 3T f m 3a a 5 NNdE NZ a 32221: a
PATENTEUHAREI I972 SHEET 120F 46 n. r I I! PATENTEDHARZI I972 SHEET 130F 16 PATENTEBMARZI I972 SHEET 1ROF46 SHEET 150F 56 g a m PATENTEDMAR 21 I972 PATENTEUHARZI I972 SHEET 190F 46 w g ..l 5 o: M m g

Claims (39)

1. In a system for continuous processing of a work throughput transported in a substantially continuous tier therethrough between two isolated atmospheres: a transition zone for interconnecting said two isolated atmospheres having a substantially constant composition comprising A. a series of alternate inlet and outlet compartments having openings for a. non-contact passage of said workpieces therethrough, b. having a cross section substantially complementary to the cross section of said workpieces to define a restricted orifice-size clearance therebetween; and c. said series comprising a minimum of three said compartments; B. inlet means adapted for providing a non-reactive gas in said inlet compartments at a pressure at least as high as the pressures of said atmospheres and having progressively increased pressures form opposite ends of said transition zone toward the interior thereof; C. outlet means adapted for exhausting gases from said outlet compartments; and D. means for transporting said workpieces in said tier from one of said atmospheres through said compartments to the other of said atmospheres.
7. The system of claim 1 where said transition zone comprises five compartments defining two of said outlet compartments and three of said inlet compartments with two of said inlet compartments disposed at opposite ends of said transition zone adjacent corresponding ones of said atmospheres, with A. said inlet means adapted to provide the pressure in said two inlet compartments at least equal to the pressures of adjacent ones of said atmospheres; B. the inlet means of the third of said inlet compartments being adapted to maintain the pressure therein at a level substantially greater than the pressures in said two inlet compartments; and C. the said outlet means adapted to maintain the pressure in said outlet compartments substantially lower than the pressures in adjacent ones of said inlet compartments.
9. In a system for continuous processing of work throughput transported in a substantially continuous tier therethrough between two atmospheres, A. a transition zone interconnecting two atmospheres and comprising an alternate series of inlet and outlet compartments for a non-reactive gas; with said series comprising a minimum of three said compartments; B. means adapted for providing a non-reactive gas in said inlet compartmeNts at a positive pressure at least as high as said pressures of said atmospheres; C. gas exhaust means for withdrawing gases from said outlet compartments to maintain pressures therein below the said pressures in said inlet compartments and of said atmospheres with said positive pressures being progressively increased from the opposite ends of said transition zone toward the interior thereof; and D. means for non-contact transport of said workpiece in said tier from one of said atmospheres through said compartments to the other of said atmospheres.
10. In a processing system for continuous processing of workpieces transported in a substantial tier therethrough between two isolated distinct atmospheres at a pressure at least as high as ambient pressures and having a substantially constant concentration, an isolation chamber interconnected with said atmospheres and comprising A. spaced end walls defining said chamber and having openings for non-contact transport of said tier of said workpieces therethrough from one of said atmospheres to the other of said atmospheres with said openings having a cross section complementary to the cross section of said tier to form a restricted orifice-size clearance therebetween; B. baffle means in said isolation chamber extending transversely thereof and subdividing said chamber into at least three alternate inlet and outlet zones and defining a series of non-contact openings aligned with the openings defined in said end walls; C. means for providing a non-reactive atmosphere in said inlet zones at a positive pressure; and D. means for withdrawing gases from said outlet zones with a. the pressure in said outlet zone adjacent a said end wall maintained lower than the pressure of an adjacent one of said atmospheres, and b. with the pressure in a said inlet zone adjacent a said inlet wall maintained at a level at least equal to the pressure of an adjacent atmosphere, and c. with the positive pressures progressively increasing from adjacent said opposite end walls toward the interior of said isolation chamber.
11. A reactor for continuous processing of workpieces transported in a substantially continuous tier therethrough comprising an open ended tube with the opposite ends thereof exposed to ambient atmosphere, partitions within said tube extending transversely thereof and defining at least three consecutive chambers comprising A. a first reactive chamber; B. an intermediate isolation chamber, and C. a second reactive chamber with said partitions provided with passageways having a cross section substantially complementary to the cross section of said tier to define a restricted orifice-type non-contact clearance therebetween providing resistance to flow of gases therethrough, and interconnecting said chambers; D. a first gas flow means for providing a flow of a reactive gas a. at a first positive pressure level at least as high as ambient pressures, and b. at a substantially constant concentration in a first of said reaction chambers; E. second gas flow means for providing a flow of a second reactive gas a. at a substantially constant concentration, and b. at a second positive pressure at least as high as ambient pressure in a second of said reactive chambers; F. baffle means in said isolation chamber defining therein at least three compartments comprising alternate inlet and outlet compartments for a non-reactive gas; G. third gas flow means for injecting and withdrawing a non-reactive gas in, respectively, said inlet and outlet compartments to provide a. the gas pressure in a said outlet compartment adjacent a said atmosphere lower than the gas pressure in said inlet compartments and at least equal to both said reactive chambers, and b. the gas pressure in said inlet compartments at a positive pressure greater than the gas pressures in both said reactive chambers with the said pressures progressively Increasing from adjacent ends of said isolation chamber toward the interior thereof.
15. The reactor of claim 11 wherein said baffles define three consecutive compartments comprising, sequentially A. a first outlet compartment adjacent said first reactive chamber; B. an intermediate inlet compartment; C. a second outlet compartment adjacent the second said reactive chamber; D. means for introducing a non-reactive atmosphere in said inlet compartments at a pressure greater than the pressures in said first and second reactive chambers; E. means for withdrawing gas from said first and second outlet compartments to maintain pressure therein less than the pressures in said inlet compartment and in said first and second reactive chambers; and F. means for transporting said tier of workpieces from said first reactive chamber through said isolation chamber into said second reactive chamber.
23. A system for processing a moving tier of workpieces comprising A. a reactive chamber; B. means for maintaining a substantially constant reactive first atmosphere in said chamber; C. means for isolating said chamber from a second atmosphere comprising an isolation chamber having a. a first opening communicating with said reactive chamber and having a cross section complementary to said tier of workpieces to form a non-contact restricted orifice-size clearance therebetween, non-contact b. a second opening communicating with said second atmosPhere with said first and second openings having a cross section corresponding to said tier of workpieces to form a non-contact restricted orifice-size clearance therebetween; D. baffle means in said isolation chamber extending transversely thereof and subdividing said isolation chamber into a series of alternate inlet and outlet compartments for a non-reactive atmosphere with said series comprising a minimum of three said compartments; E. means for providing a non-reactive atmosphere in said inlet compartments at a positive pressure at least equal to the pressure in said reactive chambers; F. means for withdrawing gases from said outlet compartments to maintain pressures therein at a level substantially lower than the pressures in said inlet compartments and and in said reactive chambers; and G. means for moving said tier of workpieces from said first reactive chamber through said isolation chamber into said second reactive chamber.
25. The system of claim 23 wherein said baffle means subdivide said chamber into five compartments comprising, sequentially, A. a first inlet compartment adjacent said first reactive chamber; B. a first outlet compartment; C. a second inlet compartment; D. a second outlet compartment; E. a third inlet compartment adjacent the said second atmosphere; F. means for providing a non-reactive atmosphere in said first and third inlet compartments at a pressure at least equal to the pressure of said first and second atmospheres; G. means for providing a non-reactive atmosphere in said second inlet compartment at a pressure substantially greater than the pressure in said first and third inlet compartments; and H. means for withdrawing gases from said outlet compartments to maintain a pressure therein substantially lower than the pressure in adjacent ones of said inlet compartments.
26. The system of claim 24 wherein adjacent ones of said pressures conform to the generalized orifice equation flow K Square Root Delta P and wherein A. the flow F1 between the first atmosphere at a pressure P1 and the first said adjacent outlet compartment at a pressure P42 2 conforms to the equation F1 K1 Square Root P1-P2 where P1 is selected to maintain a flow selected from the group consisting of a. zero flow between P1 and P2 and b. positive flow from P1 to P2 B. the flow F2 between the first said outlet compartment at said pressure P2 and said inlet compartment at a pressure P3 is greater than said flow F1 and conforms to the equation F2 K2 Square Root P3-P2 where P3 is greater than P2 and selected to maintain a positive flow from P3 to P2 C. the flow F3 between said inlet compartment at its said pressure P3 and the second said outlet compartment at a pressure P4 conforms to the equation F3 K3 Square Root P3-P4 where P4 is less than P3 and selected to maintain a positive flow from P3 to P4 D. the flow F4 between said outlet compartment at a said pressure P4 and said second atmosphere adjaCent thereto at a pressure P5 is less than the said flow F3 and conforms to the equation F4 K4 Square Root P5-P4 where P5 is selected to maintain a flow selected from the group consisting of a. zero flow between P5 and P4 and b. positive flow from P5 to P4.
27. The system of claim 25 wherein adjacent said pressures conform to the generalized orifice equation flow K Square Root Delta P and wherein A. the flow F1 between the first atmosphere at a pressure P1 and the first said inlet compartment adjacent thereto at a pressure P2 conforms to the equation F1 K1 Square Root P2-P1 where P2 is selected to maintain a gas flow selected from the groups consisting of a. zero flow between P2 and P1 and b. positive flow from P2 to P1 B. the flow F2 between the first said inlet compartment at said pressure P2 and the first said outlet adjacent the compartment at a pressure P3 conforms to the equation F2 K2 Square Root P2-P3 where a. F2 is greater than F1 b. P3 is smaller than P2 and c. P3 is selected to maintain positive flow from P2 to P3 C. where the flow F3 between said first outlet compartment at said pressure P3 and the adjacent said second inlet compartment thereto at a pressure P4 conforms to the equation F3 K3 Square Root P4-P3 where a. P4 is greater than P3 and P2 and b. P3 is selected to maintain a positive flow F3 from P4 to P3. D. the flow F4 between the second said inlet compartment at said pressure P4 and the adjacent second said outlet compartment at a pressure P5 conforms to the equation F4 K4 Square Root P4-P5 where P4 is greater than P5 and selected to maintain a positive flow F4 from P4 to P5 E. the flow F5 between the second said outlet compartment at said pressure P5 and the next succeeding third said inlet compartment at a pressure P6 conforms to the orifice equation F5 K5 Square Root P6-P5 where a. P6 is greater than P5 b. P6 is lower than P4 and c. P6 is selected to maintain a positive flow from P6 to P5 and E. the flow F6 between the third said inlet compartment at its said pressure P6 and the adjacent second of said atmosphere at a pressure P7 conforms to the generalized orifice equation F6 K6 Square Root P6-P7 where a. p6 is greater than P7 and b. P6 is selected to maintain said flow F6 selected from the group consisting of
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Cited By (37)

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US4048955A (en)*1975-09-021977-09-20Texas Instruments IncorporatedContinuous chemical vapor deposition reactor
US4268977A (en)*1979-12-031981-05-26Exxon Research & Engineering CompanySealing apparatus for ovens
US4938834A (en)*1988-03-231990-07-03Mitsubishi Denki Kabushiki KaishaApparatus for preventing the oxidation of lead frames during bonding
US5736199A (en)*1996-12-051998-04-07Northeastern UniversityGating system for continuous pressure infiltration processes
WO2000003422A3 (en)*1998-07-132000-08-03Applied Komatsu Technology IncGas flow control in a substrate processing system
US6387777B1 (en)*1998-09-022002-05-14Kelly T. HurleyVariable temperature LOCOS process
US6620288B2 (en)*2000-03-222003-09-16Semiconductor Energy Laboratory Co., Ltd.Substrate treatment apparatus
US6623686B1 (en)2000-09-282003-09-23Bechtel Bwxt Idaho, LlcSystem configured for applying a modifying agent to a non-equidimensional substrate
US6652654B1 (en)*2000-09-272003-11-25Bechtel Bwxt Idaho, LlcSystem configured for applying multiple modifying agents to a substrate
US20040058293A1 (en)*2002-08-062004-03-25Tue NguyenAssembly line processing system
US6799588B1 (en)*1999-07-212004-10-05Steag Microtech GmbhApparatus for treating substrates
US20050272266A1 (en)*2000-12-282005-12-08Tadahiro OhmiSemiconductor device and its manufacturing method
US20070224348A1 (en)*2006-03-262007-09-27Planar Systems, Inc.Atomic layer deposition system and method for coating flexible substrates
US20070281089A1 (en)*2006-06-052007-12-06General Electric CompanySystems and methods for roll-to-roll atomic layer deposition on continuously fed objects
US20070298188A1 (en)*2006-06-262007-12-27Tokyo Electron LimitedSubstrate processing method and apparatus
US20080138964A1 (en)*2006-12-122008-06-12Zhiyuan YeFormation of Epitaxial Layer Containing Silicon and Carbon
US20080182397A1 (en)*2007-01-312008-07-31Applied Materials, Inc.Selective Epitaxy Process Control
US20090074905A1 (en)*2007-09-132009-03-19The Boeing CompanyMethod and apparatus for resin transfer molding composite parts
US20100151131A1 (en)*2008-12-122010-06-17Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer-readable storage medium
US20100206235A1 (en)*2008-05-302010-08-19Alta Devices, Inc.Wafer carrier track
US20110033612A1 (en)*2001-10-262011-02-10Seagate Technology LlcDisc vapor lubrication
US20110039026A1 (en)*2009-08-112011-02-17Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer readable storage medium
US7941937B2 (en)*2002-11-262011-05-17Lg Electronics Inc.Laundry dryer control method
US20110229720A1 (en)*2010-03-162011-09-22The Boeing CompanyMethod and Apparatus For Curing a Composite Part Layup
US20120180725A1 (en)*2011-01-172012-07-19Furukawa Electric Co., Ltd.Cvd apparatus
US8375758B1 (en)2007-09-132013-02-19The Boeing CompanyInduction forming of metal components with slotted susceptors
US20130140455A1 (en)*2011-05-272013-06-06Dsa Detection LlcMulti-dopant permeation tube
US20130180452A1 (en)*2012-01-182013-07-18Tokyo Electron LimitedFilm deposition apparatus
US8556619B2 (en)2007-09-132013-10-15The Boeing CompanyComposite fabrication apparatus
US8637117B2 (en)2009-10-142014-01-28Lotus Applied Technology, LlcInhibiting excess precursor transport between separate precursor zones in an atomic layer deposition system
US20140102368A1 (en)*2012-10-122014-04-17Institute Of Nuclear Energy Research Atomic Energy Council, Executive YuanGas isolation chamber and plasma deposition apparatus thereof
US20140352889A1 (en)*2013-05-292014-12-04Spts Technologies LimitedApparatus for processing a semiconductor workpiece
US8985911B2 (en)2009-03-162015-03-24Alta Devices, Inc.Wafer carrier track
US20150101494A1 (en)*2012-10-172015-04-16Micah SaccamannoPortable Food Dehydrator
US20150184294A1 (en)*2009-12-252015-07-02Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer-readable storage medium
US20170244006A1 (en)*2014-09-192017-08-24Applied Materials, Inc.Parallel plate inline substrate processing tool
NL2029733A (en)*2021-01-272022-08-05China Triumph Int Eng Co LtdSystem with a process chamber having two process compartments with a vacuum pressure barrier in between and method for operating such a system

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Cited By (60)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4048955A (en)*1975-09-021977-09-20Texas Instruments IncorporatedContinuous chemical vapor deposition reactor
US4268977A (en)*1979-12-031981-05-26Exxon Research & Engineering CompanySealing apparatus for ovens
US4938834A (en)*1988-03-231990-07-03Mitsubishi Denki Kabushiki KaishaApparatus for preventing the oxidation of lead frames during bonding
US5736199A (en)*1996-12-051998-04-07Northeastern UniversityGating system for continuous pressure infiltration processes
US6035925A (en)*1996-12-052000-03-14Northeastern UniversityGating system for continuous pressure infiltration processes
WO2000003422A3 (en)*1998-07-132000-08-03Applied Komatsu Technology IncGas flow control in a substrate processing system
US6286230B1 (en)1998-07-132001-09-11Applied Komatsu Technology, Inc.Method of controlling gas flow in a substrate processing system
US6387777B1 (en)*1998-09-022002-05-14Kelly T. HurleyVariable temperature LOCOS process
US6799588B1 (en)*1999-07-212004-10-05Steag Microtech GmbhApparatus for treating substrates
US6620288B2 (en)*2000-03-222003-09-16Semiconductor Energy Laboratory Co., Ltd.Substrate treatment apparatus
US6962731B2 (en)2000-09-272005-11-08Bechtel Bwxt Idaho, LlcSystem configured for applying multiple modifying agents to a substrate
US20040058085A1 (en)*2000-09-272004-03-25Propp W. AlanSystem configured for applying multiple modifying agents to a substrate
US6652654B1 (en)*2000-09-272003-11-25Bechtel Bwxt Idaho, LlcSystem configured for applying multiple modifying agents to a substrate
US7241340B2 (en)2000-09-282007-07-10Battelle Energy Alliance, LlcSystem configured for applying a modifying agent to a non-equidimensional substrate
US6623686B1 (en)2000-09-282003-09-23Bechtel Bwxt Idaho, LlcSystem configured for applying a modifying agent to a non-equidimensional substrate
US20050272266A1 (en)*2000-12-282005-12-08Tadahiro OhmiSemiconductor device and its manufacturing method
US20110033612A1 (en)*2001-10-262011-02-10Seagate Technology LlcDisc vapor lubrication
US8808793B2 (en)*2001-10-262014-08-19Seagate Technology LlcDisc vapor lubrication
US20040058293A1 (en)*2002-08-062004-03-25Tue NguyenAssembly line processing system
US7941937B2 (en)*2002-11-262011-05-17Lg Electronics Inc.Laundry dryer control method
US9238868B2 (en)2006-03-262016-01-19Lotus Applied Technology, LlcAtomic layer deposition method for coating flexible substrates
US9469901B2 (en)*2006-03-262016-10-18Lotus Applied Techonology, LlcAtomic layer deposition method utilizing multiple precursor zones for coating flexible substrates
US20120219708A1 (en)*2006-03-262012-08-30Lotus Applied Technology, LlcAtomic layer deposition method utilizing multiple precursor zones for coating flexible substrates
US20100189900A1 (en)*2006-03-262010-07-29Lotus Applied Technology, LlcAtomic layer deposition system and method utilizing multiple precursor zones for coating flexible substrates
US8202366B2 (en)2006-03-262012-06-19Lotus Applied Technology, LlcAtomic layer deposition system utilizing multiple precursor zones for coating flexible substrates
US20070224348A1 (en)*2006-03-262007-09-27Planar Systems, Inc.Atomic layer deposition system and method for coating flexible substrates
US8137464B2 (en)2006-03-262012-03-20Lotus Applied Technology, LlcAtomic layer deposition system for coating flexible substrates
US20070281089A1 (en)*2006-06-052007-12-06General Electric CompanySystems and methods for roll-to-roll atomic layer deposition on continuously fed objects
US20070298188A1 (en)*2006-06-262007-12-27Tokyo Electron LimitedSubstrate processing method and apparatus
US7877895B2 (en)*2006-06-262011-02-01Tokyo Electron LimitedSubstrate processing apparatus
US8181356B2 (en)2006-06-262012-05-22Tokyo Electron LimitedSubstrate processing method
US7897495B2 (en)2006-12-122011-03-01Applied Materials, Inc.Formation of epitaxial layer containing silicon and carbon
US20080138964A1 (en)*2006-12-122008-06-12Zhiyuan YeFormation of Epitaxial Layer Containing Silicon and Carbon
US9064960B2 (en)*2007-01-312015-06-23Applied Materials, Inc.Selective epitaxy process control
US20080182397A1 (en)*2007-01-312008-07-31Applied Materials, Inc.Selective Epitaxy Process Control
US8708691B2 (en)2007-09-132014-04-29The Boeing CompanyApparatus for resin transfer molding composite parts
US8372327B2 (en)*2007-09-132013-02-12The Boeing CompanyMethod for resin transfer molding composite parts
US8375758B1 (en)2007-09-132013-02-19The Boeing CompanyInduction forming of metal components with slotted susceptors
US10543647B2 (en)2007-09-132020-01-28The Boeing CompanyApparatus for curing a composite part layup
US8556619B2 (en)2007-09-132013-10-15The Boeing CompanyComposite fabrication apparatus
US20090074905A1 (en)*2007-09-132009-03-19The Boeing CompanyMethod and apparatus for resin transfer molding composite parts
US20100206235A1 (en)*2008-05-302010-08-19Alta Devices, Inc.Wafer carrier track
US9169554B2 (en)*2008-05-302015-10-27Alta Devices, Inc.Wafer carrier track
US20100151131A1 (en)*2008-12-122010-06-17Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer-readable storage medium
US8985911B2 (en)2009-03-162015-03-24Alta Devices, Inc.Wafer carrier track
US20110039026A1 (en)*2009-08-112011-02-17Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer readable storage medium
US8637117B2 (en)2009-10-142014-01-28Lotus Applied Technology, LlcInhibiting excess precursor transport between separate precursor zones in an atomic layer deposition system
US20150184294A1 (en)*2009-12-252015-07-02Tokyo Electron LimitedFilm deposition apparatus, film deposition method, and computer-readable storage medium
US8865050B2 (en)2010-03-162014-10-21The Boeing CompanyMethod for curing a composite part layup
US20110229720A1 (en)*2010-03-162011-09-22The Boeing CompanyMethod and Apparatus For Curing a Composite Part Layup
US20120180725A1 (en)*2011-01-172012-07-19Furukawa Electric Co., Ltd.Cvd apparatus
US9275842B2 (en)*2011-05-272016-03-01Dsa Detection LlcMulti-dopant permeation tube
US20130140455A1 (en)*2011-05-272013-06-06Dsa Detection LlcMulti-dopant permeation tube
US9589778B2 (en)2011-05-272017-03-07Dsa Detection LlcMulti-dopant permeation tube with two chambers for introducing dopants into a spectrometry system
US20130180452A1 (en)*2012-01-182013-07-18Tokyo Electron LimitedFilm deposition apparatus
US20140102368A1 (en)*2012-10-122014-04-17Institute Of Nuclear Energy Research Atomic Energy Council, Executive YuanGas isolation chamber and plasma deposition apparatus thereof
US20150101494A1 (en)*2012-10-172015-04-16Micah SaccamannoPortable Food Dehydrator
US20140352889A1 (en)*2013-05-292014-12-04Spts Technologies LimitedApparatus for processing a semiconductor workpiece
US20170244006A1 (en)*2014-09-192017-08-24Applied Materials, Inc.Parallel plate inline substrate processing tool
NL2029733A (en)*2021-01-272022-08-05China Triumph Int Eng Co LtdSystem with a process chamber having two process compartments with a vacuum pressure barrier in between and method for operating such a system

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