JP2019528418A - 燃料の添加にともなう熱化学蓄熱 - Google Patents
燃料の添加にともなう熱化学蓄熱 Download PDFInfo
- Publication number
- JP2019528418A JP2019528418A JP2019501462A JP2019501462A JP2019528418A JP 2019528418 A JP2019528418 A JP 2019528418A JP 2019501462 A JP2019501462 A JP 2019501462A JP 2019501462 A JP2019501462 A JP 2019501462A JP 2019528418 A JP2019528418 A JP 2019528418A
- Authority
- JP
- Japan
- Prior art keywords
- regenerator
- oxygen
- furnace
- reaction mixture
- fuel
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
Images
Classifications
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
- C03B5/237—Regenerators or recuperators specially adapted for glass-melting furnaces
-
- 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
- C01B3/344—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 non-catalytic solid particles
-
- 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
- C01B3/36—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 oxygen or mixtures containing oxygen as gasifying agents
- C01B3/363—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 oxygen or mixtures containing oxygen as gasifying agents characterised by the burner used
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B3/00—Hearth-type furnaces, e.g. of reverberatory type; Tank furnaces
- F27B3/10—Details, accessories, or equipment peculiar to hearth-type furnaces
- F27B3/26—Arrangements of heat-exchange apparatus
- F27B3/263—Regenerators
- F27B3/266—Exhaust gases reversing flow devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D99/00—Subject matter not provided for in other groups of this subclass
- F27D99/0001—Heating elements or systems
- F27D99/0033—Heating elements or systems using burners
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0211—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step
- C01B2203/0216—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step containing a non-catalytic steam reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0211—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step
- C01B2203/0222—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step containing a non-catalytic carbon dioxide reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0435—Catalytic purification
- C01B2203/044—Selective oxidation of carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/047—Composition of the impurity the impurity being carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0872—Methods of cooling
- C01B2203/0883—Methods of cooling by indirect heat exchange
-
- 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
- C01B3/36—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 oxygen or mixtures containing oxygen as gasifying agents
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
- F27D2017/007—Systems for reclaiming waste heat including regenerators
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
-
- 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
- Y02P20/10—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
- Feeding And Controlling Fuel (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
(A)炉内で燃料を燃焼させ、酸素を含むガス状燃焼生成物を生成する工程と、
(B)あるいは、
(1)(i)炉を出たガス状燃焼生成物の一部を第1のチャンバーに通し、炭化水素燃料を第1のチャンバーに供給し、第1のチャンバー内の炭化水素燃料をガス状燃焼生成物中に存在する酸素と反応させることで、第1のチャンバー内の酸素濃度を低減させ、酸素及び0〜20,000ppm以下の一酸化炭素を含むガス状反応混合物を生成する工程と、
(ii)第1のチャンバーを出たガス状反応混合物を、冷却された第1の蓄熱器に通し、通過させることで、第1の蓄熱器を加熱し、当該ガス状反応混合物を冷却する工程と、
(iii)当該第1の蓄熱器からの当該冷却されたガス状反応混合物の少なくとも一部及び燃料を、加熱された第2の蓄熱器に通し、第2の蓄熱器において、吸熱反応時に第2の蓄熱器においてガス状反応混合物と燃料を反応させ、水素及び一酸化炭素を含む合成ガスを形成する工程と、
(iv)第2の蓄熱器において形成された当該合成ガスを当該炉内に通し、当該炉内に注入された1種類以上の酸化剤ストリームと当該合成ガスを燃焼させる工程と、
(2)(i)炉を出たガス状燃焼生成物の一部を第2のチャンバーに通し、炭化水素燃料を第2のチャンバーに供給し、第2のチャンバー内の炭化水素燃料をガス状燃焼生成物中に存在する酸素と反応させることで、第2のチャンバー内の酸素濃度を低減させ、酸素及び0〜20,000ppm以下の一酸化炭素を含むガス状反応混合物を生成する工程と、
(ii)第2のチャンバーを出たガス状反応混合物を、冷却された第2の蓄熱器に通し、通過させることで、第2の蓄熱器を加熱し、当該ガス状反応混合物を冷却する工程と、
(iii)当該第2の蓄熱器からの当該冷却されたガス状反応混合物の少なくとも一部及び燃料を、加熱された第1の蓄熱器に通し、第1の蓄熱器において、吸熱反応時に第1の蓄熱器においてガス状反応混合物と燃料を反応させ、水素及び一酸化炭素を含む合成ガスを形成する工程と、
(iv)第1の蓄熱器において形成された当該合成ガスを当該炉内に通し、当該炉内に注入された1種類以上の酸化剤ストリームと合成ガスを燃焼させる工程と、を含む。
Claims (14)
- 炉内の燃焼を実施する方法であって、
(A)炉内で燃料を燃焼させ、酸素を含むガス状燃焼生成物を生成する工程と、
(B)あるいは、
(1)(i)前記炉を出た前記ガス状燃焼生成物の一部を第1のチャンバーに通し、炭化水素燃料を前記第1のチャンバーに供給し、前記第1のチャンバー内の炭化水素燃料を前記ガス状燃焼生成物中に存在する酸素と反応させることで、前記第1のチャンバー内の酸素濃度を低減させ、酸素及び0〜20,000ppm以下の一酸化炭素を含むガス状反応混合物を生成する工程と、
(ii)前記第1のチャンバーを出た前記ガス状反応混合物を、冷却された第1の蓄熱器に通し、通過させることで、前記第1の蓄熱器を加熱し、前記ガス状反応混合物を冷却する工程と、
(iii)前記第1の蓄熱器からの前記冷却されたガス状反応混合物の少なくとも一部及び燃料を、加熱された第2の蓄熱器に通し、前記第2の蓄熱器において、吸熱反応時に前記第2の蓄熱器において前記ガス状反応混合物と燃料を反応させ、水素及び一酸化炭素を含む合成ガスを形成する工程と、
(iv)前記第2の蓄熱器において形成された前記合成ガスを前記炉内に通し、前記炉内に注入された1種類以上の酸化剤ストリームと前記合成ガスを燃焼させる工程と、
(2)(i)前記炉を出た前記ガス状燃焼生成物の一部を第2のチャンバーに通し、炭化水素燃料を前記第2のチャンバーに供給し、前記第2のチャンバー内の炭化水素燃料を前記ガス状燃焼生成物中に存在する酸素と反応させることで、前記第2のチャンバー内の酸素濃度を低減させ、酸素及び0〜20,000ppm以下の一酸化炭素を含むガス状反応混合物を生成する工程と、
(ii)前記第2のチャンバーを出た前記ガス状反応混合物を、冷却された第2の蓄熱器に通し、通過させることで、前記第2の蓄熱器を加熱し、前記ガス状反応混合物を冷却する工程と、
(iii)前記第2の蓄熱器からの前記冷却されたガス状反応混合物の少なくとも一部及び燃料を、加熱された第1の蓄熱器に通し、前記第1の蓄熱器において、吸熱反応時に前記第1の蓄熱器においてガス状反応混合物と燃料を反応させ、水素及び一酸化炭素を含む合成ガスを形成する工程と、
(iv)前記第1の蓄熱器において形成された前記合成ガスを前記炉内に通し、前記炉内に注入された1種類以上の酸化剤ストリームと前記合成ガスを燃焼させる工程と、を含む、方法。 - 工程(B)(1)(i)及び(B)(2)(i)において前記第1及び第2のチャンバーに交互に通される前記ガス燃焼生成物が、5%(v/v)超の酸素を含み、前記第1及び第2のチャンバーにおいて交互に形成される前記ガス状反応混合物が、5%(v/v)以下の酸素、及び0〜3000ppm以下の一酸化炭素を含む、請求項1に記載の方法。
- 前記第1及び第2のチャンバーで交互に形成される前記ガス状反応混合物が、0.5〜2.0%(v/v)の酸素を含む、請求項2に記載の方法。
- 工程(B)(1)(i)及び(B)(2)(i)において前記第1及び第2のチャンバーで交互に形成される前記ガス状反応混合物が、20,000ppm未満の酸素、及び少なくとも1000ppmの一酸化炭素を含む、請求項1に記載の方法。
- 工程(B)(1)(i)及び(B)(2)(i)において前記第1及び第2のチャンバーで交互に形成される前記ガス状反応混合物が、1,000ppm未満の酸素、及び1,000〜50,000ppmの一酸化炭素を含む、請求項4に記載の方法。
- 前記第1の蓄熱器、若しくは前記第2の蓄熱器、又は両方の蓄熱器から通過される前記冷却されたガス状反応混合物は、酸素と反応し、中に存在する一酸化炭素及び炭化水素の量を低減させる、請求項1に記載の方法。
- 前記酸素との反応により、前記冷却されたガス状反応混合物中の一酸化炭素の量を500ppm未満に低減させる、請求項6に記載の方法。
- 前記酸素との反応により、前記冷却されたガス状反応混合物中の一酸化炭素の量を200ppm未満に低減させる、請求項6に記載の方法。
- 前記酸素との反応により、前記冷却されたガス状反応混合物中の一酸化炭素の量を100ppm未満に低減させる、請求項6に記載の方法。
- 工程(A)及び(B)における前記炉内の燃焼は、少なくとも50%(v/v)の酸素を含む酸化剤を用いて実施される、請求項1に記載の方法。
- 工程(A)及び(B)における前記炉内の燃焼は、少なくとも80%(v/v)の酸素を含む酸化剤を用いて実施される、請求項1に記載の方法。
- 前記炉は、空気燃料バーナー及び/又は空気加熱蓄熱器の一方又は両方における燃焼によって更に加熱される、請求項1に記載の方法。
- 熱化学蓄熱器に侵入する煙道ガス中のCO2とH2Oを合わせた濃度は、少なくとも35%(v/v)である、請求項12に記載の方法。
- 熱化学蓄熱器に侵入する煙道ガス中のCO2とH2Oを合わせた濃度は、50%(v/v)超である、請求項12に記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201662362649P | 2016-07-15 | 2016-07-15 | |
US62/362,649 | 2016-07-15 | ||
PCT/US2017/041315 WO2018013455A1 (en) | 2016-07-15 | 2017-07-10 | Thermochemical regeneration with fuel additions |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2019528418A true JP2019528418A (ja) | 2019-10-10 |
Family
ID=59579904
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2019501462A Pending JP2019528418A (ja) | 2016-07-15 | 2017-07-10 | 燃料の添加にともなう熱化学蓄熱 |
Country Status (10)
Country | Link |
---|---|
US (1) | US10112860B1 (ja) |
EP (1) | EP3484812A1 (ja) |
JP (1) | JP2019528418A (ja) |
KR (1) | KR20190025975A (ja) |
CN (1) | CN109641745A (ja) |
BR (1) | BR112019000365A2 (ja) |
CA (1) | CA3030679A1 (ja) |
MX (1) | MX2019000436A (ja) |
RU (1) | RU2708603C1 (ja) |
WO (1) | WO2018013455A1 (ja) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10712092B2 (en) | 2017-03-29 | 2020-07-14 | Praxair Technology, Inc. | Reduction of regenerator clogging |
MX2021003132A (es) | 2018-10-16 | 2021-05-14 | Praxair Technology Inc | Metodo de reciclado de gases de combustion para regeneracion termoquimica. |
US11912608B2 (en) | 2019-10-01 | 2024-02-27 | Owens-Brockway Glass Container Inc. | Glass manufacturing |
Citations (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB756191A (en) * | 1953-02-16 | 1956-08-29 | Didier Werke Ag | Process for the production of hydrocarbon-free gas from gaseous hydrocarbons or hydrocarbon-containing gases, or from oil |
JPS5527859A (en) * | 1978-08-17 | 1980-02-28 | Central Glass Co Ltd | Decreasing method for nitrogen oxides in glass melting kiln exhaust gas |
JPS55154327A (en) * | 1979-05-21 | 1980-12-01 | Agency Of Ind Science & Technol | Method for reduction of nox in glass melting furnace |
JPH04231328A (ja) * | 1990-07-02 | 1992-08-20 | Air Prod And Chem Inc | ガラス製造の一貫処理法 |
JPH0517303U (ja) * | 1991-08-16 | 1993-03-05 | 石川島播磨重工業株式会社 | デイーゼル機関の廃熱回収ボイラ |
JPH06239617A (ja) * | 1992-11-27 | 1994-08-30 | Pilkington Glass Ltd | 再生ガラス炉を稼働させる方法、CO放出量を減少させる方法、再生ガラス炉及び廃ガス中のNOx含有量を減少させる方法 |
JPH08208240A (ja) * | 1995-02-01 | 1996-08-13 | Osaka Gas Co Ltd | ガラス溶解炉 |
JP2000024489A (ja) * | 1998-04-29 | 2000-01-25 | Praxair Technol Inc | 熱化学再生的熱回収プロセス |
JP2001010822A (ja) * | 1999-06-25 | 2001-01-16 | Nippon Electric Glass Co Ltd | ガラスの溶融方法 |
JP2002285234A (ja) * | 2001-03-23 | 2002-10-03 | Tokyo Gas Co Ltd | 蓄熱燃焼炉および蓄熱燃焼炉における雰囲気制御方法 |
JP2004107139A (ja) * | 2002-09-18 | 2004-04-08 | Tokyo Gas Co Ltd | ガラス溶解炉の運転方法 |
JP2006046319A (ja) * | 2004-06-30 | 2006-02-16 | Jfe Holdings Inc | 廃熱回収装置、廃熱回収システム及び廃熱回収方法 |
JP2010248079A (ja) * | 2009-04-10 | 2010-11-04 | Mitsubishi Chemicals Corp | 芳香族カルボン酸の製造方法 |
JP2011195386A (ja) * | 2010-03-19 | 2011-10-06 | Taiyo Nippon Sanso Corp | ガラス溶解炉およびガラス溶解炉における排ガスの処理方法 |
WO2011152024A1 (ja) * | 2010-05-31 | 2011-12-08 | 日本板硝子株式会社 | ガラス製品の製造方法および製造装置 |
US8425870B2 (en) * | 2008-06-18 | 2013-04-23 | Praxair Technology, Inc. | Reduction of CO and NOx in full burn regenerator flue gas |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU1208026A1 (ru) * | 1984-12-06 | 1986-01-30 | Научно-Производственное Объединение "Техэнергохимпром" | Устройство дл использовани тепла отход щих газов стекловаренной печи |
US7833009B2 (en) * | 2004-09-10 | 2010-11-16 | Air Products And Chemicals, Inc. | Oxidant injection method |
US7799314B2 (en) | 2005-09-09 | 2010-09-21 | Exxonmobil Research And Engineering Company | Hydrogen production and use in an internal combustion engine system |
US10184659B2 (en) | 2015-04-15 | 2019-01-22 | Praxair Technology, Inc. | Low-NOx combustion method |
PL3283823T3 (pl) | 2015-04-16 | 2020-01-31 | Praxair Technology, Inc. | Sposoby spalania dla strumienia paliwa o niskiej prędkości |
US10533743B2 (en) * | 2015-06-18 | 2020-01-14 | Praxair Technology, Inc. | Thermochemical regeneration with soot formation |
US10458712B2 (en) * | 2015-08-28 | 2019-10-29 | Praxair Technology, Inc. | Thermochemical regeneration with oxidant preheating |
-
2017
- 2017-07-07 US US15/643,559 patent/US10112860B1/en not_active Expired - Fee Related
- 2017-07-10 CN CN201780051615.9A patent/CN109641745A/zh active Pending
- 2017-07-10 WO PCT/US2017/041315 patent/WO2018013455A1/en unknown
- 2017-07-10 CA CA3030679A patent/CA3030679A1/en not_active Abandoned
- 2017-07-10 JP JP2019501462A patent/JP2019528418A/ja active Pending
- 2017-07-10 EP EP17751160.7A patent/EP3484812A1/en not_active Withdrawn
- 2017-07-10 KR KR1020197003242A patent/KR20190025975A/ko not_active Application Discontinuation
- 2017-07-10 RU RU2019102745A patent/RU2708603C1/ru active
- 2017-07-10 BR BR112019000365-7A patent/BR112019000365A2/pt not_active IP Right Cessation
- 2017-07-10 MX MX2019000436A patent/MX2019000436A/es unknown
Patent Citations (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB756191A (en) * | 1953-02-16 | 1956-08-29 | Didier Werke Ag | Process for the production of hydrocarbon-free gas from gaseous hydrocarbons or hydrocarbon-containing gases, or from oil |
JPS5527859A (en) * | 1978-08-17 | 1980-02-28 | Central Glass Co Ltd | Decreasing method for nitrogen oxides in glass melting kiln exhaust gas |
JPS55154327A (en) * | 1979-05-21 | 1980-12-01 | Agency Of Ind Science & Technol | Method for reduction of nox in glass melting furnace |
JPH04231328A (ja) * | 1990-07-02 | 1992-08-20 | Air Prod And Chem Inc | ガラス製造の一貫処理法 |
JPH0517303U (ja) * | 1991-08-16 | 1993-03-05 | 石川島播磨重工業株式会社 | デイーゼル機関の廃熱回収ボイラ |
JPH06239617A (ja) * | 1992-11-27 | 1994-08-30 | Pilkington Glass Ltd | 再生ガラス炉を稼働させる方法、CO放出量を減少させる方法、再生ガラス炉及び廃ガス中のNOx含有量を減少させる方法 |
JPH08208240A (ja) * | 1995-02-01 | 1996-08-13 | Osaka Gas Co Ltd | ガラス溶解炉 |
US6113874A (en) * | 1998-04-29 | 2000-09-05 | Praxair Technology, Inc. | Thermochemical regenerative heat recovery process |
JP2000024489A (ja) * | 1998-04-29 | 2000-01-25 | Praxair Technol Inc | 熱化学再生的熱回収プロセス |
JP2001010822A (ja) * | 1999-06-25 | 2001-01-16 | Nippon Electric Glass Co Ltd | ガラスの溶融方法 |
JP2002285234A (ja) * | 2001-03-23 | 2002-10-03 | Tokyo Gas Co Ltd | 蓄熱燃焼炉および蓄熱燃焼炉における雰囲気制御方法 |
JP2004107139A (ja) * | 2002-09-18 | 2004-04-08 | Tokyo Gas Co Ltd | ガラス溶解炉の運転方法 |
JP2006046319A (ja) * | 2004-06-30 | 2006-02-16 | Jfe Holdings Inc | 廃熱回収装置、廃熱回収システム及び廃熱回収方法 |
US8425870B2 (en) * | 2008-06-18 | 2013-04-23 | Praxair Technology, Inc. | Reduction of CO and NOx in full burn regenerator flue gas |
JP2010248079A (ja) * | 2009-04-10 | 2010-11-04 | Mitsubishi Chemicals Corp | 芳香族カルボン酸の製造方法 |
JP2011195386A (ja) * | 2010-03-19 | 2011-10-06 | Taiyo Nippon Sanso Corp | ガラス溶解炉およびガラス溶解炉における排ガスの処理方法 |
WO2011152024A1 (ja) * | 2010-05-31 | 2011-12-08 | 日本板硝子株式会社 | ガラス製品の製造方法および製造装置 |
Also Published As
Publication number | Publication date |
---|---|
EP3484812A1 (en) | 2019-05-22 |
US10112860B1 (en) | 2018-10-30 |
MX2019000436A (es) | 2019-06-20 |
BR112019000365A2 (pt) | 2019-04-24 |
RU2708603C1 (ru) | 2019-12-09 |
WO2018013455A1 (en) | 2018-01-18 |
CA3030679A1 (en) | 2018-01-18 |
CN109641745A (zh) | 2019-04-16 |
KR20190025975A (ko) | 2019-03-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6570207B2 (ja) | ガラス炉における熱化学再生及び熱回収 | |
JP6542912B2 (ja) | 低nox燃焼方法 | |
KR102093002B1 (ko) | 노에서 연소를 수행하는 방법 | |
WO2016205579A1 (en) | Thermochemical regeneration with soot formation | |
US20230243591A1 (en) | Regenerators with pressurized cavity in partition walls | |
JP2019528418A (ja) | 燃料の添加にともなう熱化学蓄熱 | |
KR102082061B1 (ko) | 산화제 예열을 이용한 열화학적 재생 | |
US11543183B2 (en) | Flue gas recycle method for thermochemical regeneration | |
US10611976B2 (en) | Thermochemical regeneration with superadiabatic flame temperature |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20190222 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20190307 |
|
RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20190522 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20200227 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20200317 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20201013 |