DK2913297T3 - Befugter, anlæg til ændring af naturgas, og som er forsynet hermed og fremgangsmåde til drift af befugteren - Google Patents
Befugter, anlæg til ændring af naturgas, og som er forsynet hermed og fremgangsmåde til drift af befugteren Download PDFInfo
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- DK2913297T3 DK2913297T3 DK13849858.9T DK13849858T DK2913297T3 DK 2913297 T3 DK2913297 T3 DK 2913297T3 DK 13849858 T DK13849858 T DK 13849858T DK 2913297 T3 DK2913297 T3 DK 2913297T3
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- heat exchanger
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- 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
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- 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
- C01B3/384—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 the catalyst being continuously externally heated
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L53/00—Heating of pipes or pipe systems; Cooling of pipes or pipe systems
- F16L53/30—Heating of pipes or pipe systems
- F16L53/32—Heating of pipes or pipe systems using hot fluids
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- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
-
- 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
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a 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
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
-
- 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
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
- C01B2203/1058—Nickel catalysts
-
- 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
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
-
- 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
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/6416—With heating or cooling of the system
- Y10T137/6579—Circulating fluid in heat exchange relationship
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- 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)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Claims (5)
1. Befugter (20, 30, 60), som omfatter: en strømningsbane, ad hvilken et første fluidum kan strømme; en eller flere varmevekslerenheder (22a-c), som er anbragt i en strømningsretning på strømningsbanen for det første fluidum, og hvor disse en eller flere første varmevekslerenheder (22a-c) er således udformet, at den (de) kan fremkalde en varmeveksling mellem det første fluidum og et antal fluider; en anden varmevekslerenhed (23), som er anbragt på en nedstrøms side af de en eller flere første varmevekslerenheder (22a-c) i strømningsretningen for det første fluidum, hvilken anden varmevekslerenhed (23) er således udformet, at den kan forårsage varmeveksling mellem et tredje fluidum og det første fluidum efter at have passeret gennem de en eller flere første varmevekslere (22a-c), en befugtningsenhed (26a-d), som er således udformet, at den kan tilføre vand til det første fluidum, som strømmer gennem strømningsbanen på opstrømssiderne, i strømningsretningen i strømningsbanen for det første fluidum i de en eller flere første varmevekslerenheder (22a-c) og den anden varmevekslerenhed; og en transportbane (25), som er således udformet, at den kan føre det tredje fluidum - efter at dette tredje fluidum er blevet udsat for varmeveksling i den anden varmevekslerenhed (23) - fra den anden varmevekslerenhed (23) til opstrømsside, i strømningsretningen ad strømningsbanen for det første fluidum, hørende til de en eller flere første varmevekslerenheder (22a-c), så at det tredje fluidum kan bringes til at flyde ind på strømningsbanen som det første fluidum, og hvor udformningen er en sådan, at det under driften gælder, at det første fluidum i den eller de første varmevekslerenheder (22a-c) opvarmes og be-fugtes, og at det andet fluidum kan køles og udleveres udadtil; og således, at det i den anden opvarmningsenhed (23) gælder, at det første fluidum kan opvarmes og befugtes til mætningsdamptryk og afleveres udvendigt, og det tredje fluidum kan køles.
2. Befugter (20, 30) ifølge krav 1, hvor strømningsbanen er én søjle (21), som kan give plads til de en eller flere varmevekslerenheder (22a, 22b, 22c) og den anden varmevekslerenhed (23).
3. Befugter (60) ifølge krav 1, hvor strømningsbanen er rør (62a, 62b) til forbindelse af et antal beholdere (61a-c) med hinanden; og hvor de en eller flere første varmevekslerenheder (22a, 22b, 22c) og den anden varmevekslerenhed (23) er rummet i de respektive beholdere (61a-c).
4. Anlæg (1) til ændring af naturgas, og som omfatter: en befugter (20; 30; 60), som beskrevet i ethvert af kravene 1 til 3; en reformenhed (2) til at få naturgas, som udgør det første fluidum, til at reagere med vanddamp med henblik på fremstilling af en syntetisk gas, som kan udgøre det andet fluidum, og som indeholder hydrogen, carbonmo-nooxid og carbondioxid; og en naturgas-forsyningsledning (10) til levering afen naturgas, som udgør det tredje fluidum.
5. Fremgangsmåde til drift af en befugter (20; 30; 60) ifølge ethvert af kravene 1 til 3, og som omfatter: at man lader et første fluidum flyde ad en første bane; at der tilvejebringes varmeveksling mellem dette første fluidum og et andet fluidum ved en eller flere første varmevekslerenheder (22a-c); at der ved den anden varmevekslerenhed (23) tilvejebringes en varmeveksling mellem et tredje fluidum og det første fluidum, efter at det første fluidum er blevet ledt gennem de(n) første varmevekslerenhed(er) (22a-c); at der ved hjælp af en befugtningsenhed eller befugtningsenheder (26a-d) tilføres vand til det første fluidum, som strømmer gennem strømningsbanen på de opstrøms sider, langs strømningsretningen for det første fluidums strømningsbane i forbindelse med de en eller flere første varmevekslerenheder (22a-c) og den anden varmevekslerenhed (23); og at der via en transportbane (25) ledes et tredje fluidum, efter at sidstnævnte er blevet udsat for varmeveksling i den anden varmevekslerenhed (23) fra den anden varmevekslerenhed (23) til det første fluidums opstrømsside i de en eller flere første varmevekslerenheder (22a-c), idet man fører det tredje fluidum ind på strømningsbanen som det første fluidum; og at der i de en eller flere første varmevekslerenheder (22a-c) foretages en opvarmning og befugtning af det første fluidum, og det andet fluidum afkøles og afgives udadtil; og at det i den anden varmevekslerenhed (23) gælder, at det første fluidum opvarmes og befugtes til mætningsdamptrykket og afgives udadtil, og det tredje fluidum afkøles.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2012236672A JP5925105B2 (ja) | 2012-10-26 | 2012-10-26 | サチュレータ及びこれを備える天然ガス改質システム |
PCT/JP2013/073924 WO2014065020A1 (ja) | 2012-10-26 | 2013-09-05 | サチュレータ及びこれを備える天然ガス改質システム |
Publications (1)
Publication Number | Publication Date |
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DK2913297T3 true DK2913297T3 (da) | 2018-03-26 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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DK13849858.9T DK2913297T3 (da) | 2012-10-26 | 2013-09-05 | Befugter, anlæg til ændring af naturgas, og som er forsynet hermed og fremgangsmåde til drift af befugteren |
Country Status (8)
Country | Link |
---|---|
US (1) | US9638367B2 (da) |
EP (1) | EP2913297B1 (da) |
JP (1) | JP5925105B2 (da) |
AU (1) | AU2013335985B2 (da) |
CA (1) | CA2888593C (da) |
DK (1) | DK2913297T3 (da) |
RU (1) | RU2598934C1 (da) |
WO (1) | WO2014065020A1 (da) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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JP6362126B2 (ja) | 2013-03-11 | 2018-07-25 | 三菱重工エンジニアリング株式会社 | メタノールプラント及びガソリン合成プラント |
WO2019139847A2 (en) | 2018-01-09 | 2019-07-18 | Advanced Building Systems, Inc. | Advanced curtain wall top-down renovation |
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EP0849245A1 (en) | 1996-12-20 | 1998-06-24 | Kvaerner Process Technology Limited | Process and plant for the production of methanol |
CA2292178C (en) | 1998-12-07 | 2003-07-15 | Mitsubishi Heavy Industries, Ltd. | Method of manufacturing methanol |
JP2000313601A (ja) * | 1999-04-26 | 2000-11-14 | Ishikawajima Harima Heavy Ind Co Ltd | ガス化炉への酸化剤供給装置 |
AU2001233112A1 (en) * | 2000-02-01 | 2001-08-14 | Texaco Development Corporation | Integration of shift reactors and hydrotreaters |
DE10059910C2 (de) * | 2000-12-01 | 2003-01-16 | Daimler Chrysler Ag | Vorrichtung zur kontinuierlichen Befeuchtung und Entfeuchtung der Zuluft von Fertigungsprozessen oder Raumlufttechnik-Anlagen |
JP4706812B2 (ja) * | 2000-12-25 | 2011-06-22 | 三菱瓦斯化学株式会社 | ジメチルエーテルの製造方法 |
JP4959074B2 (ja) * | 2001-07-19 | 2012-06-20 | 三菱重工業株式会社 | メタノールの製造方法 |
US7069981B2 (en) * | 2002-11-08 | 2006-07-04 | Modine Manufacturing Company | Heat exchanger |
JP4175921B2 (ja) * | 2003-03-12 | 2008-11-05 | 東京瓦斯株式会社 | 水素製造装置における熱回収システム |
WO2005056150A2 (en) * | 2003-12-03 | 2005-06-23 | Arizona Board Of Regents | Method and apparatus for simultaneous heat and mass transfer utilizing a carrier-gas at various absolute pressures |
EP1570901B1 (en) * | 2004-03-01 | 2008-08-13 | Haldor Topsoe A/S | Process for cooling an exothermic reaction zone and reactor unit |
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DE102007019830B3 (de) * | 2007-04-25 | 2008-07-31 | Uhde Gmbh | Primärreformer mit brennerzuführenden Sekundäreinlasskanälen |
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EP2401052B1 (en) * | 2009-02-24 | 2013-11-27 | Cyril Timmins | Improved method for the capture and disposal of carbon dioxide in an energy conversion process |
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2012
- 2012-10-26 JP JP2012236672A patent/JP5925105B2/ja active Active
-
2013
- 2013-09-05 EP EP13849858.9A patent/EP2913297B1/en active Active
- 2013-09-05 US US14/437,076 patent/US9638367B2/en active Active
- 2013-09-05 DK DK13849858.9T patent/DK2913297T3/da active
- 2013-09-05 AU AU2013335985A patent/AU2013335985B2/en active Active
- 2013-09-05 WO PCT/JP2013/073924 patent/WO2014065020A1/ja active Application Filing
- 2013-09-05 CA CA2888593A patent/CA2888593C/en active Active
- 2013-09-05 RU RU2015115158/05A patent/RU2598934C1/ru active
Also Published As
Publication number | Publication date |
---|---|
RU2598934C1 (ru) | 2016-10-10 |
AU2013335985A1 (en) | 2015-04-30 |
WO2014065020A1 (ja) | 2014-05-01 |
JP2014084265A (ja) | 2014-05-12 |
EP2913297B1 (en) | 2017-12-13 |
US9638367B2 (en) | 2017-05-02 |
EP2913297A1 (en) | 2015-09-02 |
EP2913297A4 (en) | 2016-06-29 |
CA2888593A1 (en) | 2014-05-01 |
US20150276112A1 (en) | 2015-10-01 |
JP5925105B2 (ja) | 2016-05-25 |
CA2888593C (en) | 2017-10-24 |
AU2013335985B2 (en) | 2016-01-07 |
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