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Patent US5385689A successfully refreshed from Google Patents.
US5385689A
Expired / Lapsed
US
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Process and composition for purifying semiconductor process gases to remove Lewis acid and oxidant impurities therefrom
Assignee: Entegris Inc
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Filing: 1993-06-29
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Granted: 1995-01-31
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Expires: 2013-06-29
Abstract
Abstract Scavenger compositions useful for purifying process gas streams, such as process gas streams, such as hydrogen, nitrogen, noble gases, diborane, and hydride gases from Groups IVA-VIA of the Periodic Table, such as arsine, phosphine, silane, germane, hydrogen selenide, and hydrogen telluride, and mixtures thereof, to remove water, oxygen, and other oxidant and Lewis acid impurities therefrom, such scavenger comprising a porous, high surface area inert support having thereon an active scavenging species, formed by the deposition on the support of a Group IA metal and pyrolysis thereof at a selected elevated temperature on said support. In another aspect, the present invention relates to a method of making a scavenger useful for purifying process gas streams, to remove water, oxygen, and other oxidant and Lewis acid impurities therefrom, and a process for purifying process gas streams to remove water, oxygen, and other oxidant and Lewis acid impurities therefrom, such process comprising contacting the impurity-containing process gas stream with a scavenger of the general type described above. In a further aspect, the invention relates to a method for using scavengers of the general type described above as back-diffusion scrubbers to protect the manufacturing process or gas supply system from inadvertent introduction of impurities, such method comprising contacting the impurity-containing process gas stream with a scavenger of the general type described above and providing in the scavenger bed one or more endpoint detectors so that back-diffusion events are observed.
Inventors
- 👤 Glenn M. Tom
- 👤 James V. McManus
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:53
CPC Classifications
E; E02; E02F; E02F9/00; E02F9/20; E02F9/22; E02F9/2221; E02F9/2232; E02F9/2235; B; B01; B01D; B01D53/00; B01D53/26; B01D53/28; B01D53/34; B01D53/38; B01D53/40; B01D53/46; B01J; B01J20/00; B01J20/02; B01J20/28; B01J20/28054; B01J20/28057; B01J20/28078; B01J20/30; B01J20/32; B01J20/3202; B01J20/3206; B01J20/3208; B01J20/321; B01J20/3231; B01J20/3234; B01J20/3236; E02F9/2278; E02F9/2282; E02F9/2296
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
142 words
A scavenger having utility for purifying a gaseous mixture comprising (i) a primary component selected from one or more members of the group consisting of hydrogen, nitrogen, noble gases, diborane and Group IVA-VIA hydride gases, and (ii) impurities selected from one or more members of the group consisting of Lewis acids and oxidants, said scavenger comprising: an inert support having a surface area in the range of from about 50 to about 1000 square meters per gram, and thermally stable up to at least about 250° C.; and an active scavenging species, present on the support at a concentration of from about 0.01 to about 1.0 moles per liter of support, and formed by the deposition on the support of a Group IA metal selected from sodium, potassium, rubidium, and cesium and their mixtures and alloys and pyrolysis thereof on said support.
Claim 2
Dependent Claim
142 words
A scavenger having utility for purifying a gaseous mixture comprising (i) a primary component selected from one or more members of the group consisting of hydrogen, nitrogen, noble gases, diborane and Group IVA-VIA hydride gases, and (ii) impurities selected from one or more members of the group consisting of Lewis acids and oxidants, said scavenger comprising: an inert support having a surface area in the range of from about 50 to about 1000 square meters per gram, and thermally stable up to at least about 250° C.; and an active scavenging species, present on the support at a concentration of from about 0.01 to about 1.0 moles per liter of support, and formed by the deposition on the support of a Group IA metal selected from sodium, potassium, rubidium, and cesium and their mixtures and alloys and pyrolysis thereof on said support.
Claim 3
Dependent Claim
32 words
A scavenger according to claim 1, wherein said support is a macroreticulate polymer formed from monomers selected from the group consisting of styrene, vinyltoluene, vinylisopropylbenzene, ethylvinylbenzene, vinylnaphthalene, alpha-methylstyrene, beta-methylstyrene, and mixtures thereof.
Claim 4
Dependent Claim
33 words
A scavenger according to claim 2, wherein the polymer has been formed by polymerization of said monomer in the presence of a cross-linking agent selected from the group consisting of divinylbenzene and divinylnaphthalene.
Claim 5
Dependent Claim
11 words
A scavenger according to claim 1, wherein said support is poly(styrenedivinylbenzene).
Claim 6
Dependent Claim
34 words
A scavenger according to claim 1, wherein the support has pores of a diameter in the range of from about 3 to about 200 Ångstroms, and is thermally stable up to about 250° C.
Claim 7
Dependent Claim
29 words
A scavenger according to claim 1, having a water removal capacity of from about 0.2 to about 20 liters gaseous water per liter of a bed of said scavenger.
Claim 8
Dependent Claim
29 words
A scavenger according to claim 1, having an oxygen removal capacity of from about 0.2 to about 20 liters gaseous water per liter of a bed of said scavenger.
Claim 9
Dependent Claim
23 words
A scavenger according to claim 1, wherein the Group IA metal is selected from the group consisting of sodium, potassium, and sodium-potassium alloys.
Claim 10
Dependent Claim
31 words
A scavenger according to claim 8, wherein the Group IA metal is present on the support at a concentration of from about 0.01 to about 0.25 moles per liter of support.
Claim 11
Dependent Claim
31 words
A scavenger according to claim 1 wherein said scavenger in said purification process produces an effluent gas stream having a concentration of less than 60 ppb C 1 -C 4 hydrocarbons.
Claim 12
Independent Claim
165 words
A method of making a scavenger having utility for purifying a gaseous mixture comprising (i) a primary component selected from one or more members of the group consisting of hydrogen, nitrogen, noble gases, diborane and Group IVA-VIA hydride gases, and (ii) impurities selected from one or more members of the group consisting of Lewis acids and oxidants, to remove said impurities therefrom, said method comprising: providing a support having a surface area in the range of from about 50 to about 1000 square meters per gram, and thermally stable up to at least about 250° C.; depositing on such support, at a concentration from about 0.01 to about 1.0 moles per liter of support, a Group IA metal selected from the group consisting of sodium, potassium, rubidium and cesium and mixtures and alloys thereof; and pyrolyzing the metal on the support, at a temperature of from about 125° C. to about 225° C. under sufficient conditions to distribute the alkali metal throughout the porous support.
Claim 13
Independent Claim
165 words
A method of making a scavenger having utility for purifying a gaseous mixture comprising (i) a primary component selected from one or more members of the group consisting of hydrogen, nitrogen, noble gases, diborane and Group IVA-VIA hydride gases, and (ii) impurities selected from one or more members of the group consisting of Lewis acids and oxidants, to remove said impurities therefrom, said method comprising: providing a support having a surface area in the range of from about 50 to about 1000 square meters per gram, and thermally stable up to at least about 250° C.; depositing on such support, at a concentration from about 0.01 to about 1.0 moles per liter of support, a Group IA metal selected from the group consisting of sodium, potassium, rubidium and cesium and mixtures and alloys thereof; and pyrolyzing the metal on the support, at a temperature of from about 125° C. to about 225° C. under sufficient conditions to distribute the alkali metal throughout the porous support.
Claim 14
Dependent Claim
35 words
A method as in claim 11, wherein during the step of pyrolyzing the metal on the support, the support is blanketed with an inert gas selected from the group consisting of argon, nitrogen, and helium.
Claim 15
Dependent Claim
31 words
A method according to claim 11, wherein the Group IA metal is deposited on the support in a concentration of from about 0.01 to about 0.25 moles per liter of support.
Claim 16
Dependent Claim
22 words
A method as in claim 11, wherein said sufficient conditions to distribute the alkali metal throughout the porous support comprise intermittent mixing.
Claim 17
Dependent Claim
22 words
A method as in claim 11, wherein said sufficient conditions to distribute the alkali metal throughout the porous support comprise continuous mixing.
References Cited (Backward Citations)
US4603148A
Cited
US4604270A
Cited
US4800189A
Cited
US4659552A
Cited
US4761395A
Cited
US4781900A
Cited
US4853148A
Cited
US4925646A
Cited
US4950419A
Cited
US4983363A
Cited
US5015411A
Cited
US4797227A
Cited
US4865822A
Cited
EP0365490A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1998-01-30 | 1998-08-01 | 1999-01-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2002-01-30 | 2002-08-01 | 2003-01-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2006-01-30 | 2006-08-01 | 2007-01-31 | $7700.00 | Window Closed / Lapsed |