PH12017550143A1 - Synthesis gas production method and apparatus - Google Patents

Synthesis gas production method and apparatus

Info

Publication number
PH12017550143A1
PH12017550143A1 PH12017550143A PH12017550143A PH12017550143A1 PH 12017550143 A1 PH12017550143 A1 PH 12017550143A1 PH 12017550143 A PH12017550143 A PH 12017550143A PH 12017550143 A PH12017550143 A PH 12017550143A PH 12017550143 A1 PH12017550143 A1 PH 12017550143A1
Authority
PH
Philippines
Prior art keywords
synthesis gas
biogas
production method
pretreatment
gas production
Prior art date
Application number
PH12017550143A
Inventor
Kazuyuki Fujimoto
Takanori KAIGAWA
Original Assignee
Air Water Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Air Water Inc filed Critical Air Water Inc
Publication of PH12017550143A1 publication Critical patent/PH12017550143A1/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/40—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts characterised by the catalyst
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Catalysts (AREA)

Abstract

The present invention provides a synthesis gas production method for generating a synthesis gas having an H2/CO molar ratio of approximately 1-2, using a biogas as a raw material without a pretreatment for removing CO2. In production of the synthesis gas containing carbon monoxide and hydrogen as main components by allowing a reforming reaction of a hydrocarbon-type gas, an oxygen-type gas, and steam to take place, a biogas is used as the hydrocarbon-type gas, and carbon dioxide is not separated out when the biogas undergoes the reforming reaction. The synthesis gas containing carbon monoxide and hydrogen as main components is generated using the biogas as a raw material without a pretreatment thereof. A desired synthesis gas can be obtained without spending costs or consuming power for a CO2 removal step such as PSA.
PH12017550143A 2015-06-17 2017-12-15 Synthesis gas production method and apparatus PH12017550143A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2015121594A JP2017007872A (en) 2015-06-17 2015-06-17 Synthesis gas production process and apparatus
PCT/JP2016/066110 WO2016203944A1 (en) 2015-06-17 2016-06-01 Synthesis gas production method and apparatus

Publications (1)

Publication Number Publication Date
PH12017550143A1 true PH12017550143A1 (en) 2018-06-11

Family

ID=57545673

Family Applications (1)

Application Number Title Priority Date Filing Date
PH12017550143A PH12017550143A1 (en) 2015-06-17 2017-12-15 Synthesis gas production method and apparatus

Country Status (3)

Country Link
JP (1) JP2017007872A (en)
PH (1) PH12017550143A1 (en)
WO (1) WO2016203944A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102097283B1 (en) * 2017-03-16 2020-04-06 한국과학기술연구원 Method for preparing synthetic natural gas having improved caloric value and application for the same
US10738247B2 (en) 2017-11-15 2020-08-11 Gas Technology Institute Processes and systems for reforming of methane and light hydrocarbons to liquid hydrocarbon fuels
KR102528025B1 (en) * 2017-11-15 2023-05-03 가스 테크놀로지 인스티튜트 Noble metal catalysts and methods for reforming methane and other hydrocarbons
WO2020054063A1 (en) * 2018-09-14 2020-03-19 株式会社 ユーリカ エンジニアリング Synthetic gas production system for low-carbon ft synthetic oil production
US12122962B2 (en) 2018-09-18 2024-10-22 Gti Energy Processes and catalysts for reforming of impure methane-containing feeds
CN111547678B (en) * 2020-04-08 2022-03-25 华南农业大学 Method and system for preparing methanol by full-component thermal catalysis of marsh gas

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4663104B2 (en) * 2000-12-06 2011-03-30 石油資源開発株式会社 Syngas production by autothermal reforming
JP4666985B2 (en) * 2004-09-28 2011-04-06 国立大学法人北見工業大学 Equipment for direct cracking of lower hydrocarbons
US7906559B2 (en) * 2007-06-21 2011-03-15 University Of Southern California Conversion of carbon dioxide to methanol and/or dimethyl ether using bi-reforming of methane or natural gas
JP5731202B2 (en) * 2010-03-08 2015-06-10 エア・ウォーター株式会社 Syngas production method and apparatus
BR112013000541A2 (en) * 2010-07-09 2016-05-24 Haldor Topsoe As process to convert biogas to a methane rich gas
US9339797B2 (en) * 2011-06-08 2016-05-17 Raphael Idem Sulfur tolerant catalysts for hydrogen production by carbon dioxide reforming of methane-rich gas
JP6041162B2 (en) * 2012-08-01 2016-12-07 国立大学法人九州大学 Paper-like catalyst for reforming hydrocarbons, paper-like catalyst array, and solid oxide fuel cell having paper-like catalyst or paper-like catalyst array

Also Published As

Publication number Publication date
JP2017007872A (en) 2017-01-12
WO2016203944A1 (en) 2016-12-22

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