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US3917467A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for manufacturing high purity methane gas

Assignee: JGC Corp
•
Filing: 1973-01-08
•
Granted: 1975-11-04
•
Expires: 1993-01-08
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Abstract

Abstract A process for manufacturing high purity methane gas by subjecting a gas mixture mainly comprising methane, hydrogen, carbon monoxide, carbon dioxide and steam to a first methanization reaction step in the presence of a nickel catalyst filled in the reaction zone to methanize a part of the carbon oxides contained therein, then subjecting the gas mixture from the first step to a carbon dioxide-absorption step to remove superfluous carbon dioxide and then subjecting the gas mixture from said absorption step to a second methanization reaction step in the presence of a nickel catalyst filled in the reaction zone to methanize the residual carbon oxides.

Inventors

  • 👤 Tsutomu Toida
  • 👤 Seiichi Matsuoka
  • 👤 Kenzo Yamamoto
  • 👤 Kouji Tamura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 01:54
CPC Classifications
C; C10; C10K; C10K3/00; C10K3/02; C10K3/04; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0485; C07C9/00; C07C9/02; C07C9/04; C07C2521/00; C07C2521/06; C07C2521/08; C07C2521/10; C07C2523/00; C07C2523/16; C07C2523/24; C07C2523/26; C07C2523/32; C07C2523/34; C07C2523/70; C07C2523/72; C07C2523/74; C07C2523/755

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 235 words
A PROCESS FOR MANUFACTURING A HIGH PURITY METHANE GAS WHICH COMPRISES: PASSING A GAS MIXTURE CONSISTING ESSENTIALLY OF METHANE, STREAM, HYDROGEN, CARBON MONOXIDE AND CARBON DIOXIDE THROUGH A FIRST METHANIZATION REACTION ZONE UNDER ADIABATIC METHANIZATION REACTION CONDITIONS OF A TEMPERATURE IN THERANGE OF 250* TO 500*C AND A PRESSURE IN THE RANGE OF ATMOSPHERIC PRESSURE OF 100 JG/CM2G AND IN CONTACT WITH METHANIZATION CATALYST TO PRODUCE A FIRST INTERMEDIATE GAS, COOLING SAID FIRST INTERMEDIATE GAS TO A TEMPERATURE OF 40* TO 170*C AND REMOVING CONDENCED STREAM THERREFROM PASSING THE REMAINDER OF SAID COOLED FIRST INTERMEDIATE GAS THROUGH A CARBON DIOXIDE ABSORPTION ZONEE AND THEREIN REMOVING FROM SAID COOLED FIRST INTERMEDIATE GAS ALL OF THE CARBON DIOXIDE CONTAINED THEREIN IN EXCESS OF THE QUALITY CAPABLE OF REACTING WITH THE HYDROGEN CONTAINED IN SAID FIRST INTERMEDIATE GAS PRODUCT METHANE, WHEREBY TO 00000000 OBTAIN A SECOND INTERMEDIATE GAS FREE OF EXCESS CARBON DIOXIDE, RAISING THE TEMPERATURE OF SAID SECOND INTERMEDIATE GAS AND THEN PASSING THE ENTIRELY OF SAID SECOND INTERMEDIATE GAS THROUGH ONE OR MORE ADDITION METHANIZATION REACTION ZONES UNDER ADIABATIC METHANIZATON REACTION A CONDITIONS OF A TEMPERATURE IN THE RANGE OF ATMOSPHERIC PRESSURE CATALYST PRESSURE IN THE RANGE OF ATMOSPHERIC PRESSURE TO 100 KG/CM2 G AND IN CONTACT WITH METHANIZATION CATALYST TO METHANIZE THE REMAINAINING CARBON MONOXIDE AND CARBON DIOXIDE, AND OBTAINING FROM THE LAST OF THE METHALIZATION REACTION ZONES AN EFFULENT GAS OF HIGH PURITY METHANE.
Claim 2
Dependent Claim 235 words
A PROCESS FOR MANUFACTURING A HIGH PURITY METHANE GAS WHICH COMPRISES: PASSING A GAS MIXTURE CONSISTING ESSENTIALLY OF METHANE, STREAM, HYDROGEN, CARBON MONOXIDE AND CARBON DIOXIDE THROUGH A FIRST METHANIZATION REACTION ZONE UNDER ADIABATIC METHANIZATION REACTION CONDITIONS OF A TEMPERATURE IN THERANGE OF 250* TO 500*C AND A PRESSURE IN THE RANGE OF ATMOSPHERIC PRESSURE OF 100 JG/CM2G AND IN CONTACT WITH METHANIZATION CATALYST TO PRODUCE A FIRST INTERMEDIATE GAS, COOLING SAID FIRST INTERMEDIATE GAS TO A TEMPERATURE OF 40* TO 170*C AND REMOVING CONDENCED STREAM THERREFROM PASSING THE REMAINDER OF SAID COOLED FIRST INTERMEDIATE GAS THROUGH A CARBON DIOXIDE ABSORPTION ZONEE AND THEREIN REMOVING FROM SAID COOLED FIRST INTERMEDIATE GAS ALL OF THE CARBON DIOXIDE CONTAINED THEREIN IN EXCESS OF THE QUALITY CAPABLE OF REACTING WITH THE HYDROGEN CONTAINED IN SAID FIRST INTERMEDIATE GAS PRODUCT METHANE, WHEREBY TO 00000000 OBTAIN A SECOND INTERMEDIATE GAS FREE OF EXCESS CARBON DIOXIDE, RAISING THE TEMPERATURE OF SAID SECOND INTERMEDIATE GAS AND THEN PASSING THE ENTIRELY OF SAID SECOND INTERMEDIATE GAS THROUGH ONE OR MORE ADDITION METHANIZATION REACTION ZONES UNDER ADIABATIC METHANIZATON REACTION A CONDITIONS OF A TEMPERATURE IN THE RANGE OF ATMOSPHERIC PRESSURE CATALYST PRESSURE IN THE RANGE OF ATMOSPHERIC PRESSURE TO 100 KG/CM2 G AND IN CONTACT WITH METHANIZATION CATALYST TO METHANIZE THE REMAINAINING CARBON MONOXIDE AND CARBON DIOXIDE, AND OBTAINING FROM THE LAST OF THE METHALIZATION REACTION ZONES AN EFFULENT GAS OF HIGH PURITY METHANE.
Claim 3
Dependent Claim 32 words
A process for manufacturing high purity methane gas according to claim 1, in which said gas mixture fed to the first methanization reaction zone has a methane content above 25 vol. %.
Claim 4
Dependent Claim 70 words
A process for preparing high purity methane gas according to claim 1, in which said methanization catalyst is an activated nickel catalyst obtained by reducing at 200*-500*C a catalyst composition carried on diatomaceous earth, said catalyst composition consisting essentially of nickel oxide and 5 - 60 vol. %, based on nickel oxide, of magnesium oxide and further containing oxides of copper and chromium or oxides of copper, chromium and manganese.

References Cited (Backward Citations)

US3429680A Cited
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US3511624A Cited
US3392218A Cited
US3728093A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-11-03 1979-05-05 1979-11-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-11-03 1983-05-05 1983-11-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-11-03 1987-05-05 1987-11-04 $7700.00 Window Closed / Lapsed

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