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US3864450A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing nitrogen oxides from gaseous mixtures

Assignee: Toray Industries Inc
•
Filing: 1972-06-23
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Granted: 1975-02-04
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Expires: 1992-06-23
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Abstract

Abstract Removal of nitrogen oxides from waste gases by contacting the waste gases with hot carbon which contains sodium hydroxide and/or potassium hydroxide.

Inventors

  • 👤 Tetsu Takeyama
  • 👤 Ryoh Endoh
  • 👤 Keizo Masuda

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 19:50
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/02; B01J23/04; B01D; B01D53/00; B01D53/34; B01D53/92; B01D53/94; B01D53/9404; B01D53/9409; B01D53/9413; B01D53/9418; B01D2255/00; B01D2255/20; B01D2255/202; B01D2255/2022; B01D2255/2027; B01D2255/70; B01D2255/702

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 67 words
IN A PROCESS FOR THE REMOVAL OF A NITROGEN OXIDE IMPURITY FROM A GASEOUS MIXTURE, WHEREIN THE GASEOUS MIXTURE SUBJECTED TO THE TREATMENT CONTAINS BOTH A NITROGEN OXIDE IMPURITY AND OXYGEN, THE STEPS COMPRISING CONTACTING THE GASEOUS MIXTURE WITH A CATALYST CONSISTING ESSENTIALLY OF CARBON IMPREGNATED WITH SODIUM HYDROXIDE OR POTASSIUM HYDROXIDE, WHILE MAINTAINING SAID CATALYST AT A TEMPERATURE IN THE RANGE FROM ABOUT 250*C. TO 480*C.
Claim 2
Dependent Claim 67 words
IN A PROCESS FOR THE REMOVAL OF A NITROGEN OXIDE IMPURITY FROM A GASEOUS MIXTURE, WHEREIN THE GASEOUS MIXTURE SUBJECTED TO THE TREATMENT CONTAINS BOTH A NITROGEN OXIDE IMPURITY AND OXYGEN, THE STEPS COMPRISING CONTACTING THE GASEOUS MIXTURE WITH A CATALYST CONSISTING ESSENTIALLY OF CARBON IMPREGNATED WITH SODIUM HYDROXIDE OR POTASSIUM HYDROXIDE, WHILE MAINTAINING SAID CATALYST AT A TEMPERATURE IN THE RANGE FROM ABOUT 250*C. TO 480*C.
Claim 3
Dependent Claim 18 words
The process according to claim 1 wherein the reaction temperature is between about 350* C and 450* C.
Claim 4
Dependent Claim 38 words
The process according to claim 1 wherein the concentration of said alkali metal hydroxide contained in the carbon catalyst is from about 2.0 to 20.0 percent by weight of metal based upon the weight of the original carbon.
Claim 5
Dependent Claim 21 words
The process according to claim 1 wherein the carbon is selected from the group consisting of coke, semi-coke, and petroleum coke.
Claim 6
Dependent Claim 34 words
The process according to claim 1 wherein the gaseous mixture is passed through the catalyst bed at a space velocity from about 6,000 to 80,000 volumes of gas per volume of catalyst per hour.

References Cited (Backward Citations)

US2992895A Cited
US3552912A Cited
US3715187A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-02-03 1978-08-05 1979-02-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-02-03 1982-08-05 1983-02-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-02-03 1986-08-05 1987-02-04 $7700.00 Window Closed / Lapsed

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