A filter includes at least two different adsorptive media. first, chemisorptive media, which is porous and includes an acidic functional group, is used to remove molecular bases, including ammonia, organic amines, imides and aminoalchols, from the atmosphere used in semiconductor fabrication and other processes that require uncontaminated gaseous environments of high quality. second, physisorptive media is able to adsorb condensable contaminants, particularly those having a boiling point greater than 150 degrees C. The physisorptive media can include untreated, activated carbon.

Patent
   RE44536
Priority
May 05 2000
Filed
Jun 01 2011
Issued
Oct 15 2013
Expiry
May 04 2021
Assg.orig
Entity
Large
5
123
all paid
0. 43. An apparatus for removing contaminants from a gas in a semiconductor processing device comprising:
a filter enclosure having an inlet for receiving a gas and an outlet for discharging a gas;
a filter system within the enclosure having a plurality of parallel filter elements and at least one filter element in series with at least one of the parallel filter elements, wherein filters positioned in series comprise a first filter element that filters a first contaminant and a second filter element that filters a second contaminant, and further wherein the first filter element comprises a physisorptive filter media and the second filter element comprises a chemisorptive filter media.
21. An apparatus for removing contaminants from a gas in a semiconductor processing device comprising:
a filter enclosure having an inlet for receiving a gas and an outlet for discharging a gas;
a filter system within the enclosure having a plurality of parallel filter elements and at least one filter element in series with at least one of the parallel filter elements; and
a plurality of sampling ports for sampling gas flowing through the enclosure including a sampling port positioned between the at least one filter element that is positioned in series with at least one of the parallel filter elements to collect a gas sample from the gas flowing between the filter elements positioned in series.
1. A method for removing contaminants from a gas in a semiconductor processing device comprising:
flowing a gas through an enclosure having an inlet for receiving the gas and an outlet for discharging the gas;
filtering the gas in the enclosure with a filter unit coupled to the inlet and the outlet and having a plurality of parallel filter elements located within said filter unit for removing at least a portion of said contaminants from said gas passing through said enclosure, the filter unit further comprising at least one filter element positioned in series with at least one of the parallel filter elements; and
sampling the gas with a sampling port coupled to the gas flow between filter elements positioned in series within the filter unit to collect sample data.
0. 35. A method for removing contaminants from a gas in a semiconductor processing device comprising:
flowing a gas through an enclosure having an inlet for receiving the gas and an outlet for discharging the gas;
filtering the gas in the enclosure with a filter unit coupled to the inlet and the outlet and having a plurality of parallel filter elements located within said filter unit for removing at least a portion of said contaminants from said gas passing through said enclosure, the filter unit further comprising at least one filter element positioned in series with at least one of the parallel filter elements, wherein filters positioned in series comprise a first filter element that filters a first contaminant and a second filter element that filters a second contaminant, and further wherein the first filter element comprises a physisorptive filter media and the second filter element comprises a chemisorptive filter media.
2. The method of claim 1 further comprising providing an air filtration system.
3. The method of claim 2 further comprising flowing said gas through each parallel filter element and through the at least one filter element positioned in series.
4. The method of claim 3 further comprising a providing plurality of sampling ports.
5. The method of claim 4 further comprising providing the plurality of sampling ports with an associated like plurality of filter elements.
6. The method of claim 4 further including an inlet sampling port.
7. The method of claim 4 further including an outlet sampling port.
8. The method of claim 5 further comprising removing amine contaminants.
9. The method of claim 1 further comprising coupling said sampling port to a detection system.
10. The method of claim 9 further comprising coupling an amine detection system.
11. The method of claim 1 further comprising coupling the sampling port to an analyzer that determines filter life.
12. The method of claim 11 further comprising using data from one or more ports selected from the group consisting of an inlet sampling port, a port between filters and an outlet sampling port.
13. The method of claim 1 further comprising providing filters positioned in series such that a first filter element filters a first contaminant and a second filter element filters a second contaminant.
14. The method of claim 13 further comprising providing a first filter element including a physisorptive filter media.
15. The method of claim 13 further comprising providing a second filter element including a chemisorptive filter media.
16. The method of claim 14 further comprising providing a physisorptive media including an activated carbon.
17. The method of claim 15 further comprising providing a chemisorptive media including an acidic material.
18. The method of claim 17 further comprising providing an acidic material including a sulfonated material.
19. The method of claim 17 further comprising providing an acidic material including a carboxylic functional group.
20. The method of claim 1 further comprising providing a concentrator coupled to the sampling port that accumulates a contaminant.
22. The apparatus of claims 21 wherein said gas passing through each parallel filter element passes through the at least one filter element positioned in series.
23. The apparatus of claim 21 wherein said contaminants include amines.
24. The apparatus of claim 21 wherein said sampling port is communicatively coupled to a detection system.
25. The apparatus of claim 21 wherein the sampling port is connected to an analyzer that determines filter life.
26. The apparatus of claim 21 wherein filters positioned in series comprise a first filter element that filters a first contaminant and a second filter element that filters a second contaminant.
27. The apparatus of claim 26 wherein the first filter element comprises a physisorptive filter media.
28. The apparatus of claim 26 wherein the second filter element comprises a chemisorptive filter media.
29. The apparatus of claim 27 wherein the physisorptive media comprises an activated carbon.
30. The apparatus of claim 28 wherein the chemisorptive media comprises an acidic material.
31. The apparatus of claim 30 wherein the acidic material comprises a sulfonated material.
32. The apparatus of claim 30 wherein the acidic material comprises a carboxylic functional group.
33. The apparatus of claim 21 wherein the sampling port is coupled to a concentrator that accumulates a contaminant.
34. The apparatus of claim 21 further comprising a plurality of sampling ports between filter elements positioned in series.
0. 36. The method of claim 35 wherein the physisorptive filter media is upstream of chemisorptive filter media.
0. 37. The method of claim 36 wherein the physisorptive media comprises an activated carbon.
0. 38. The method of claim 36 wherein the chemisorptive media comprises an acidic material.
0. 39. The method of claim 38 wherein the acidic material comprises a sulfonated material.
0. 40. The method of claim 39 wherein the sulfonated material comprises a sulfonated divinyl benzene styrene copolymer.
0. 41. The method of claim 38 wherein the acidic material comprises a carboxylic functional group.
0. 42. The method of claim 36 further comprising removing amine contaminants.
0. 44. The apparatus of claim 43 wherein the physisorptive filter media is upstream of chemisorptive filter media.
0. 45. The apparatus of claim 44 wherein said contaminants include amines.
0. 46. The apparatus of claim 44 wherein the physisorptive media comprises an activated carbon.
0. 47. The apparatus of claim 44 wherein the chemisorptive media comprises an acidic material.
0. 48. The apparatus of claim 47 wherein the acidic material comprises a sulfonated material.
0. 49. The apparatus of claim 47 wherein the sulfonated material comprises a sulfonated divinyl benzene styrene copolymer.
0. 50. The apparatus of claim 49 wherein the acidic material comprises a carboxylic functional group.

The present application is a
Where R° is an organic free radical, and oxygen, O2, reacts as
O2custom character20°
Such that
Si—R°+O°custom characterSi—R—O or R—Si—O
Repeating the above reaction n-times provides
Si—R+O2custom characterSi—O2+R+R—O+ . . .
thereby producing Si—O2, which is a non-volatile inorganic oxide that is condensable on the sacrificial lens 602. Therefore, by exposing the Si—R to UV radiation, the acoustic wave detector 600 is able to detect the amount of Si—R in the sampled air.

Rather than connecting the sampling port to an analytical device, the sampling port 510 can be connected to a concentrator 524, as illustrated in FIG. 24B. A pump 526 coupled to the concentrator 524 draws the samples to the concentrator through a line 528. Alternatively, as illustrated in FIG. 24C, the sample accumulates by diffusion in a concentrator 530 attached directly to the sampling port 510. In either case, the operator takes the concentrator 524 or 530 back to the lab where the contents of the concentrator is evaluated by any of the analytical devices described above.

While this invention has been particularly shown and described with references to preferred embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the scope of the invention encompassed by the appended claims.

Kishkovich, Oleg P., Grayfer, Anatoly, Goodwin, William M., Kinkead, Devon, Ruede, David

Patent Priority Assignee Title
10278656, May 09 2016 IMAGE INSIGHT, INC Medical devices for diagnostic imaging
11020704, Mar 19 2014 MORGAN STANLEY SENIOR FUNDING, INC System and method for removing airborne molecular contaminants from gas streams
11428832, Nov 12 2012 IMAGE INSIGHT INC Crowd-sourced hardware calibration
11969273, May 09 2016 IMAGE INSIGHT, INC. Medical devices for diagnostic imaging
11980847, Mar 19 2014 Entegris, Inc. System and method for removing airborne molecular contaminants from gas streams
Patent Priority Assignee Title
2430861,
3019127,
3409691,
3607706,
3961920, Jan 24 1974 Gas adsorber cell test sampler
3998988, Dec 24 1970 Teijin Limited Conjugate fiber, fibrous material and fibrous article made therefrom and process for production thereof
4055075, Apr 08 1976 Flanders Filters, Inc. Method and apparatus for the leak testing of filters
4072793, Jul 23 1975 Asahi Kasei Kogyo Kabushiki Kaisha Reinforced ion-exchange membrane
4135896, Dec 11 1975 PROCESS SYSTEMS INTERNATIONAL, INC Gas purifier having rechargeable adsorber filter with removeable rechargeable sample canister
4204011, Jul 04 1977 Kurashiki Boseki Kabushiki Kaisha Method of driving powdery material into porous material of open-celled structure
4224415, Jul 18 1958 Rohm and Haas Company Polymerization processes and products therefrom
4313832, Jun 12 1980 Rohm and Haas Company Method for treatment of aqueous solutions with ion exchange fibers
4322230, Sep 08 1980 Donaldson Company, Inc. Unitized gas-particulate filter and housing
4549472, Sep 29 1983 Hitachi Ltd.; Hitachi Plant Engineering & Construction Co. Rearrangeable partial environmental control device
4629479, May 15 1984 Ital Idee s.r.l. Multiple filter unit
4760423, Mar 12 1987 INDIGO N V Apparatus and method for reducing hydrocarbon emissions from a liquid-based electrophotographic copying machine
4808202, Nov 27 1986 Unitka, Ltd. Adsorptive fiber sheet
4852133, Nov 07 1986 Hitachi, Ltd. X-ray lithography apparatus
4904343, Sep 26 1984 STERLING CHEMICALS INTERNATIONAL, INC Non-woven activated carbon fabric
4946480, Sep 27 1989 Filter apparatus with improved filtration and saturation level detector
4981501, Mar 02 1990 MBH FILTRATION GMBH & CO KG Adsorption filter with high air permeability
5023654, Oct 31 1988 Brother Kogyo Kabushiki Kaisha Thermal fixing device for image recording apparatus
5039321, Nov 04 1988 TOSHIBA CERAMICS CO , LTD , A JOINT-STOCK COMPANY OF JAPAN Apparatus for preventing clouding of a semiconductor wafer
5130743, Oct 23 1989 Brother Kogyo Kabushiki Kaisha Image forming apparatus having means for indicating timing of heat-fixing filter
5133864, Sep 16 1985 The Dow Chemical Company Filters employing particulate porous polymers
5143552, Mar 09 1988 Tokyo Electron Limited Coating equipment
5166530, Dec 20 1991 ULTRATECH STEPPER, INC ; ULTRATECH STEPPER EAST, INC Illuminator for microlithographic integrated circuit manufacture
5181819, Oct 09 1990 Tokyo Electron Limited Apparatus for processing semiconductors
5204055, Dec 08 1989 MASSACHUSETTS INSTITUTE OF TECHNOLOGY, A CORP OF MA Three-dimensional printing techniques
5219464, Oct 09 1990 Tokyo Electron Limited Clean air apparatus
5290345, Jan 13 1993 Donaldson Company, Inc. Refillable gas adsorption bed assembly and counterflow adsorber module
5300604, Jan 21 1992 Process for making a macroporous styrene polymer
5302354, Jun 26 1992 Pall Corporation Filtration device
5306321, Jul 07 1992 Donaldson Company, Inc. Layered air filter medium having improved efficiency and pleatability
5328758, Oct 11 1991 Minnesota Mining and Manufacturing Company Particle-loaded nonwoven fibrous article for separations and purifications
5340656, Dec 08 1989 Massachusetts Institute of Technology Three-dimensional printing techniques
5387380, Dec 08 1989 Massachusetts Institute of Technology Three-dimensional printing techniques
5399377, Dec 31 1992 The Board of Trustees of the University of Illinois; BOARD OF TRUSTEES, THE, OF THE UNIVERSITY OF ILLINOIS Borazine oligomers and composite materials including boron nitride and methods of making the same
5430303, Jul 01 1992 Nikon Corporation Exposure apparatus
5434644, May 18 1993 Tokyo Electron Limited Filter device
5459943, Feb 04 1993 Tokyo Electron Limited Air cleaning apparatus
5462485, Dec 03 1993 Mykrolis Corporation Controlling air quality
5486410, Nov 18 1992 Hollingsworth & Vose Company Fibrous structures containing immobilized particulate matter
5514196, Feb 04 1993 Tokyo Electron Limited Air cleaning apparatus
5582864, Jan 26 1994 Environmental L.L.C. Elastomeric polysulfide composites and method
5582865, Dec 12 1988 Entegris, Inc Non-woven filter composite
5605746, Nov 18 1992 Hollingsworth & Vose Company Fibrous structures containing particulate and including microfiber web
5607647, Dec 02 1993 Entegris, Inc Air filtering within clean environments
5616169, Jun 17 1994 VON BLUCHER, HASSO; DE RUITER, ERNEST Seal-free and frame-free odor and/or pollutant filter
5626820, Dec 12 1988 Entegris, Inc Clean room air filtering
5647356, Jul 28 1993 FILTRATION GROUP, INC Respirator cartridge with sealing fit test structure and method of use
5675752, Sep 15 1994 Sony Trans Com Interactive applications generator for an interactive presentation environment
5685895, Aug 10 1994 Nikon Corporation Air cleaning apparatus used for an exposure apparatus
5743927, Jul 31 1996 Donaldson Company, Inc.; Donaldson Company Air filter element; assembly; and, method
5753345, May 11 1995 Kabushiki Kaisha Seibu Giken; KUMA, TOSHIMI Adsorber for humidity and odorous gas exchange
5772738, Nov 30 1993 NOMURA MICRO SCIENCE CO , LTD Multifunctional air filter and air-circulating clean unit with the same incorporated therein
5772884, Jan 25 1993 Daikin Industries, Ltd. Porous polytetrafluoroethylene film and process for preparation thereof
5783608, Nov 22 1994 Ebara Corporation; Japan Atomic Energy Research Institute Process for producing separation functional fibers and ion-exchange fibers produced therefrom
5807424, Jun 17 1994 Blucher GmbH Regenerative adsorption filter bed for exhauster hoods
5833726, May 26 1995 Entegris, Inc Storing substrates between process steps within a processing facility
5834114, May 31 1995 Board of Trustees of the University of Illinois, The Coated absorbent fibers
5856198, Dec 28 1994 Entegris, Inc Performance monitoring of gas-phase air filters
5890367, Jul 24 1996 Samsung Electronics Co., Ltd. Air conditioning system for semiconductor clean room including a chemical filter downstream of a humidifier
5906429, Sep 02 1993 Nikon Corporation Optical illumination device
5928792, May 10 1997 Entegris, Inc Process for making surface modified porous membrane with perfluorocarbon copolymer
5944878, Apr 12 1995 AIRBITE AB Multiple-element air filter
5964927, Jul 11 1997 Donaldson Company, Inc Adsorption apparatus
6013821, Jun 25 1998 AbbVie Inc Removal of silylated compounds from solvent and gas waste streams
6033573, May 29 1997 The United States of America as represented by the Secretary of Activated nutshell carbons from agricultural waste
6056805, Aug 15 1997 GUARDIAN ENVIRONMENTAL TECHNOLOGIES, INC Method and apparatus for the absorption of non-polar organic molecules on hydrocarbon block copolymers
6096267, Feb 28 1997 Mykrolis Corporation System for detecting base contaminants in air
6162281, Dec 23 1998 Drager Sicherheitstechnik GmbH Device and process for displaying the exhaustion of a gas filter
6207460, Jan 14 1999 Mykrolis Corporation Detection of base contaminants in gas samples
6227383, May 03 1996 Blucher GmbH Filtering material and process for the production thereof, and adsorption filter produced from said filtering material
6228135, Nov 02 1992 Ebara Corporation; Japan Atomic Research Institute Purification of very slightly contaminated air within a clean room
6296806, Feb 28 1997 Mykrolis Corporation Protection of semiconductor fabrication and similar sensitive processes
6352579, Aug 05 1998 Toray Industries, Inc. Chemical filter unit and gas purification system
6398846, Oct 15 1997 MORGAN STANLEY SENIOR FUNDING, INC Semiconductor manufacturing system with getter safety device
6447584, Aug 20 1998 Entegris, Inc Filters employing porous strongly acidic polymers
6533847, Feb 13 2001 Donaldson Company, Inc Adsorption apparatus
6610128, Aug 20 1998 Entegris, Inc Filters employing porous strongly acidic polymers
6740147, May 05 2000 MORGAN STANLEY SENIOR FUNDING, INC Filters employing both acidic polymers and physical-adsorption media
6761753, May 05 2000 MORGAN STANLEY SENIOR FUNDING, INC Methods using filters employing both acidic polymers and physical-adsorption media
6770736, Sep 25 1998 Celanese Sales Germany GmbH Activated carbon filter
7014693, May 05 2000 MORGAN STANLEY SENIOR FUNDING, INC Filters employing both acidic polymers and physical-adsorption media
7022164, Aug 20 1998 MORGAN STANLEY SENIOR FUNDING, INC Filters employing porous strongly acidic polymers
7049382, Sep 25 1998 Celanese Sales Germany GmbH Activated carbon filter
7132011, Sep 02 2003 MORGAN STANLEY SENIOR FUNDING, INC Reactive gas filter
7264648, Jun 19 2003 CLEAN METHANE SYSTEMS LLC Removing siloxanes from a gas using a segmented filtration system customized to the gas composition
7540901, May 05 2000 Entegris, Inc Filters employing both acidic polymers and physical-adsorption media
7922791, Jul 13 2006 MORGAN STANLEY SENIOR FUNDING, INC Filtering system for a semiconductor processing tool
20020078828,
20020110510,
20040154470,
20060078827,
20060169139,
DE19859788,
DE4413606,
EP335034,
EP398847,
EP584030,
EP1022043,
EP1105203,
EP1402943,
JP10165730,
JP10165744,
JP10192624,
JP10216477,
JP10230117,
JP2001317000,
JP3038212,
JP4126513,
JP4575596,
JP6063333,
JP6198123,
JP8024534,
JP8168628,
RE29410, May 23 1970 C. Weinberger & Co., Ltd. Process for manufacturing of deodorizing air filters
WO7696,
WO10687,
WO25896,
WO185308,
WO2005021134,
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