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US4259303A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of and system for treating waste anesthetic gas

Assignee: KURARA Co Ltd
•
Filing: 1979-10-15
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Granted: 1981-03-31
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Expires: 1999-10-15
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Abstract

Abstract The present invention provides a method of treating a waste anesthetic gas by contacting the laughing gas contained in the waste anesthetic gas with a catalyst comprising one or more metal oxides selected from the group consisting of ferric oxide, cobalt oxide, cupric oxide, chromium oxide, manganese dioxide and nickel oxide to decompose the laughing gas into nitrogen and oxygen. This method is of practical value for preventing the neighborhood of hospitals from environmental pollution problem.

Inventors

  • 👤 Osamu Nakaji
  • 👤 Seisuke Takashima
  • 👤 Seishiro Nakamura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 22:44
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; A; A61; A61M; A61M16/00; A61M16/0087; A61M16/009; A61M16/0093; Y; Y02; Y02C; Y02C20/00; Y02C20/10; Y10; Y10S; Y10S128/00; Y10S128/91

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 65 words
A method of treating waste anesthetic gas containing laughing gas (N 2 O), comprising: passing said waste anesthetic gas over a catalyst comprising at least one metal oxide selected from the group consisting of ferric oxide, cobalt oxide, cupric oxide, chromium oxide, manganese dioxide and nickel oxide at a temperature of 250° C. to 650° C. to decompose said laughing gas to nitrogen and oxygen.
Claim 2
Independent Claim 65 words
A method of treating waste anesthetic gas containing laughing gas (N 2 O), comprising: passing said waste anesthetic gas over a catalyst comprising at least one metal oxide selected from the group consisting of ferric oxide, cobalt oxide, cupric oxide, chromium oxide, manganese dioxide and nickel oxide at a temperature of 250° C. to 650° C. to decompose said laughing gas to nitrogen and oxygen.
Claim 3
Dependent Claim 23 words
The method of claim 1, wherein said catalyst is supported on a carrier selected from the group consisting of alumina, silica and titania.
Claim 4
Dependent Claim 32 words
The method of claim 1 or 2, wherein said catalyst is a binary system catalyst comprising cupric oxide and chromium oxide, the mixing ratio by weight of cupric oxide/chromium oxide being 1/0.1-10.
Claim 5
Dependent Claim 33 words
The method of claim 3, wherein said catalyst is a ternary system catalyst comprising cupric oxide, chromium oxide and manganese dioxide, the mixing ratio by weight of cupric oxide/chromium oxide/manganese oxide being 1/0.1-10/0.05-20.
Claim 6
Dependent Claim 28 words
The method of claim 1, wherein said metal oxide catalyst is supported on a carrier in an amount of 0.1 to 50% by wt. based on said carrier.
Claim 7
Dependent Claim 17 words
The method of claim 1, wherein said temperature of decomposition ranges from 350° C. to 550° C.
Claim 8
Independent Claim 119 words
A system for treating a waste anesthetic gas, comprising: a discharge circuit for removing the waste anesthetic gas from an anesthetic circuit connected to a reactor, said reactor comprising: (a) an inlet port for receiving the waste anesthetic gas from said discharge circuit, (b) a container filled with a catalyst comprising at least one metal oxide selected from the group consisting of ferric oxide, cobalt oxide, cupric oxide, chromium oxide, manganese dioxide and nickel oxide for decomposing the laughing gas present in said waste anesthetic gas, said container being provided with a heating means for heating the laughing gas at a temperature of 250° C. to 650° C., and (c) an outlet port for discharging the decomposed gas therethrough.
Claim 9
Independent Claim 119 words
A system for treating a waste anesthetic gas, comprising: a discharge circuit for removing the waste anesthetic gas from an anesthetic circuit connected to a reactor, said reactor comprising: (a) an inlet port for receiving the waste anesthetic gas from said discharge circuit, (b) a container filled with a catalyst comprising at least one metal oxide selected from the group consisting of ferric oxide, cobalt oxide, cupric oxide, chromium oxide, manganese dioxide and nickel oxide for decomposing the laughing gas present in said waste anesthetic gas, said container being provided with a heating means for heating the laughing gas at a temperature of 250° C. to 650° C., and (c) an outlet port for discharging the decomposed gas therethrough.
Claim 10
Dependent Claim 23 words
The system of claim 7, wherein said catalyst is supported on a carrier selected from the group consisting of alumina, silica and titania.
Claim 11
Dependent Claim 32 words
The system of claim 7 or 8, wherein said catalyst is a binary system catalyst comprising cupric oxide and chronium oxide, the mixing ratio by weight of cupric oxide/chromium oxide being 1/0.1-10.
Claim 12
Dependent Claim 35 words
The system of claim 7 or 8, wherein said catalyst is a ternary system catalyst comprising cupric oxide, chromium oxide and manganese dioxide, the mixing ratio by weight of cupric oxide/chromium oxide/manganese oxide being 1/0.1-10/0.05-20.

References Cited (Backward Citations)

US2407221A Cited
US4088604A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-03-30 1984-09-29 1985-03-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-03-30 1988-09-29 1989-03-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-03-30 1992-09-29 1993-03-31 $7700.00 Window Closed / Lapsed

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