WO2008057051A1 - Groupe motopropulseur perfectionné de navire avec unité de gazéification de charbon et groupe motopropulseur à gaz de synthèse - Google Patents

Groupe motopropulseur perfectionné de navire avec unité de gazéification de charbon et groupe motopropulseur à gaz de synthèse Download PDF

Info

Publication number
WO2008057051A1
WO2008057051A1 PCT/SG2007/000380 SG2007000380W WO2008057051A1 WO 2008057051 A1 WO2008057051 A1 WO 2008057051A1 SG 2007000380 W SG2007000380 W SG 2007000380W WO 2008057051 A1 WO2008057051 A1 WO 2008057051A1
Authority
WO
WIPO (PCT)
Prior art keywords
feedstock
onboard
vessel
syngas
marine vessel
Prior art date
Application number
PCT/SG2007/000380
Other languages
English (en)
Inventor
How Kiap Gueh
Original Assignee
How Kiap Gueh
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 How Kiap Gueh filed Critical How Kiap Gueh
Priority to KR1020097011854A priority Critical patent/KR20090107488A/ko
Publication of WO2008057051A1 publication Critical patent/WO2008057051A1/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B35/00—Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for
    • B63B35/44—Floating buildings, stores, drilling platforms, or workshops, e.g. carrying water-oil separating devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63H—MARINE PROPULSION OR STEERING
    • B63H21/00—Use of propulsion power plant or units on vessels
    • B63H21/12—Use of propulsion power plant or units on vessels the vessels being motor-driven
    • B63H21/14—Use of propulsion power plant or units on vessels the vessels being motor-driven relating to internal-combustion engines
    • 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
    • C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/57—Gasification using molten salts or metals
    • 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
    • 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
    • C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
    • 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
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/12—Heating the gasifier
    • C10J2300/123—Heating the gasifier by electromagnetic waves, e.g. microwaves
    • C10J2300/1238—Heating the gasifier by electromagnetic waves, e.g. microwaves by plasma
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
    • C10J2300/1656—Conversion of synthesis gas to chemicals
    • C10J2300/1659—Conversion of synthesis gas to chemicals to liquid hydrocarbons
    • 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
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • 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
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T70/00—Maritime or waterways transport
    • Y02T70/50—Measures to reduce greenhouse gas emissions related to the propulsion system
    • Y02T70/5218—Less carbon-intensive fuels, e.g. natural gas, biofuels

Definitions

  • a feedstock material containing some carbon is first subjected to thermal conversion to yield a syngas blend comprising carbon monoxide and hydrogen (syngas), thermal conversion is supplied heat by means of a heat exchanger, exchanger further deriving thermal energy from waste heat generated by powerplant of a maritime vessel. Additional thermal energy may be added to the exchanger by means of a secondary heat source.
  • the syngas blend is then subjected to chemical conversion into a hydrocarbon product having a carbon number in the range of between C 1 to C 60 , the product is isolated, collected and stored onboard for subsequent delivery and distribution to at least one remote site.
  • US patent 4568522 discloses a synfuel production ship that produces synthetic fuel from the synthesis of carbon dioxide and hydrogen. Further disclosed is the use of a nuclear powerplant to provide energy required for the synthesis. There is no disclosure nor is anything said which suggests that the manner of synthesis involves the formation of a Syngas blend and passing the Syngas blend into a reaction to create the synthetic fuel.
  • US patent 6380268 discloses a process wherein a Syngas is formed from a feedstock using a electric-powered plasma reactor and then converting the Syngas into a higher molecular weight hydrocarbon using a Fischer-Tropsch reactor.
  • the invention can be mounted on a barge or larger vessel. Feedstock is predominantly a hydrocarbon source. There is no disclosure as to how the barge or larger vessel will interact with the invention to perform any cooling of parts of the plasma reactor, or its plant. No molten material is disclosed as a medium to cause formation of the syngas from the feedstock.
  • US patent 4181504 discloses a method for using high temperature plasma to convert carbonaceous feedstock into a Syngas, and further discloses the plasma heating a molten metal as part of the plasma's conductive electrode, and carbonaceous feedstock is fed into the molten metal by gravity for gasification into the Syngas.
  • Carbonaceous feedstock disclosed is predominantly coal. There is no disclosure nor is anything said which suggests that the invention is performed onboard a marine vessel.
  • US patent numbers 5280757, 4644877, 4431612, 6037560 discloses the use of a plasma as heat source to perform waste detoxification, treatment and decomposition. There is no disclosure nor is anything said which suggests that US patent numbers 5280757, 4644877, 4431612, 6037560 is performed onboard a marine vessel.
  • US patent 5878814 discloses a production marine vessel that converts natural gas into liquefied natural gas onboard.
  • US patents 6518321 and 6635681 discloses a process for converting a light hydrocarbon feedstock into Syngas, and then forming a syncrude hydrocarbon product using Fischer-Tropsch synthesis.
  • US patent 6797243 discloses the intake of Syngas for Fischer-Tropsch synthesis into a long- chain hydrocarbon product. Feedstock for Syngas is predominantly lighter molecular weight hydrocarbons.
  • US patent 6732796 discloses a process for in-situ conversion of hydrocarbon into Syngas, at a suitable pyrolysis conversion temperature.
  • US patent 4566961 discloses the use of an electric arc to convert carbonaceous material (coal) into lower molecular weight hydrocarbons by bringing the material into contact with the arc and further utilizing the heat of the formed hydrocarbon to implement further material conversion (of higher molecular weight carbonaceous material into lower molecular weight hydrocarbons. There is no disclosure nor is anything said which suggests that the manner of conversion utilizes a high temperature plasma as heat source.
  • US patent 4588850 discloses the use of coal in an electric arc furnace (EAF) to convert the coal into Syngas and acetylene at a pyrolysis temperature provided by the electric arc as its heat source. It further discloses that the heat can also be derived from a plasma process. There is no disclosure nor is anything said which suggests that the invention is performed onboard a marine vessel.
  • EAF electric arc furnace
  • US patent 4536603 discloses the use of coal for conversion into acetylene by using a heat source from a combustion gas.
  • US patent 4772775 discloses the use of a electric arc plasma as heat source to separate a water spray stream into hydrogen and oxygen, and having the recombined hydrogen and oxygen to form a super-heated steam product.
  • US patent 6200430 discloses the use of a three-stage electric arc gasifier process wherein synthetic gas is produced.
  • US patent 4406666 discloses gasification of carbon in a molten metal bath to produce a synthetic gas product, the molten melt bath in a reactor is made to be swivel periodically. There is no disclosure nor is anything said which suggests that the invention is performed onboard a marine vessel.
  • hydrocarbons may include methanol, light olefins, gasoline, diesel, heavy wax fuels etc.
  • Upstream technologies developed for the oil industry include marine vessels (offshore oil rigs, submersible platforms, etc.) that can drill to depths that was not possible just one decade ago, and various downstream technologies such as dedicated FPSO (floating production storage and offloading) vessels that can perform a variety of refinery and storage functions.
  • FPSO floating production storage and offloading
  • Marine vessels ranging from container ships that can travel between continents and vast distances to maritime vessels that are simply moored or anchored to body of water, such as storage platforms or ships that can function of depositories for energy assets such as crude oil, or to conduct drilling of energy reserves found deep within the depths of the sea.
  • energy assets such as crude oil
  • production vessels that can convert the extracted energy such as natural gas, into denser or more suitable forms, such as methanol, LNG, etc.
  • any floatation structure, vehicle, platform, and/or offshore platform could be operated in seawater, freshwater, or both.
  • a ship ocean-going vessel, barge, hull- vessel, hull, tanker, cargo ship, VLCC (very large crude carrier), FPSO (floating production, storage and off-loading vessel), offshore platforms (semi-submersible, submersible, "rigs") are included in this definition of marine vessel or vessel. Submarines are further included in the definition as same as the term "submersible platform” or vessel.
  • Plasma producing device or plasma producing apparatus, or plasma system
  • a plasma is a mixture of ions, electrons and neutral particles produced when stable molecules are dissociated (in this case by an electric arc).
  • the electric arc is formed between two electrodes, the anode (+) and cathode (-).
  • Variations of a plasma-producing device may be in the electrode assembly, the type of flow gas (air, argon, carbon dioxide etc.), use of plasma arc torches, and their power supply requirements (AC versus DC current etc).
  • Material, or feedstock may be in any form and can be either naturally occurring, or a synthetic material, or both, most forms of matter such as solids, liquids and gases are included in the term feedstock or material or carbonaceous material or carbonaceous feedstock.
  • MSW Municipal solid waste
  • scrap waste material sludge, marine sludge, waste oil, waste sludge, scrap metal, wood, coal, lignite, waste coal, carbon black, rubber, scrap rubber material, rubber derived material, wood chips, charcoal, glass, paper, refuse derived waste, refused derived fuel (RDF), sand, soil material, granular particles, tar s
  • a hydrocarbon product comprising a carbon number of between C 1 to C 4 , or C 5 to Ci 0 , or Ci 1 to C 2O , C 21 to C 30 , or C 31 to C 6 o
  • carbon-based fuels comprising a carbon number of between C1 to C 4 , or C 5 to Ci 0 , or C 11 to C 20 , C 21 to C 30 , or C 31 to C 6 o
  • Syngas has a heating value of between 75 to 350 BTU per cubic foot - however, BTU values will vary and may exceed the given range depending on gas element composition ratio.
  • Method of splitting into component elements may be electric, electrochemical, thermal or a combination.
  • Voltage Refers to a supply of voltage (or electric energy) and can include direct current (DC) or alternating current (AC) power. Voltage may further comprise of a particular voltage phase.
  • the prime mover device or system or engine of the vessel usually responsible for supplying propulsion power to the vessel, and may feature a mechanical system (sometimes called a marine drive) coupling the engine to the propeller shalf.
  • a mechanical system sometimes called a marine drive
  • the marine drive would be the interface wherein energy generated from the powerplant is converted into propulsion for the vessel.
  • the device or system may produce mechanical power, or electric power, or both, depending on the type of powerplant.
  • the device or system may produce mechanical power, or electric power, or both, depending on the type of powerplant.
  • a device usually comprising a furnace that utilizes an induction coil that is powered from an ac power source. Alternating current flowing through the coil creates a magnetic field that is applied to the electrically conductive charge placed inside of the furnace's crucible. Eddy currents induced by the field in the charge can be used to heat, melt and superheat the charge. Modifications and adaptations may be made to allow the conductive charge to be deployed as heating medium to perform heating of the carbonaceous feedstock according to the embodiments of the present invention.
  • a metallic material or mixture of dissimilar metals is brought together to be melted into a molten form, usually in a furnace device.
  • Metals either ferrous or non-ferrous
  • the thermal conversion plant may be in communication or operationally connected with a variety of parts and subsystems of the marine vessel, or other related plant system of the overall process of the present invention.
  • the thermal conversion plant uses mainly thermal energy to cause the conversion process, either by convection, radiation, conduction, or a combination thereof.
  • the chemical reaction unit is in communication or operationally connected with the thermal conversion plant. Conversion process may or may not make use of a catalyst material or medium to aid in the conversion process to hydrocarbon.
  • a marine vessel (such as a suitably adapted floatation vehicle) performs intake and loading of a carbonaceous feedstock up to a predetermined load tonnage, from a first remote site, which may be a port terminal facility, a second marine vessel, or a flotation terminal/structure such as an offshore platform, or a land-based/terrestrial facility.
  • the feedstock may be pre-treated including reducing or increasing its moisture content, either by heat drying (reducing moisture), or fluid spraying or steaming (increasing moisture).
  • the feedstock may also be reduced in physical size by means of a grinder device, or be pulverized into a suitable sieve size. The reduction of the feedstock will enlarge surface area that can be converted into the Syngas blend during conversion stage in the thermal conversion plant.
  • the pre-treated feedstock is then passed into the thermal conversion plant to allow for the feedstock to be thermally converted into a Syngas blend comprising CO and H 2 , however, the Syngas blend may further comprise of additional gases such as CO2 etc, depending on the proximate/ultimate analysis and composition of the feedstock used.
  • the present invention may use a mixture of different feedstock types depending on the location where the feedstock is collected for conversion).
  • the syngas blend may undergo a gas "clean-up" stage where the additional gases are removed to an acceptable level, and passed into the chemical reaction unit/plant, where the syngas is converted into a hydrocarbon product, commonly with the aid of a catalyst.
  • the choice of catalyst, reaction pressure, residency time in the reaction unit, temperature of the syngas feed-stream will determine the hydrocarbon formation of a particular molecular weight.
  • the hydrocarbon product is then isolated, or collected for storage onboard the vessel, which is then subsequently delivered and distributed to a remote site.
  • the marine vessel is simultaneously performing delivery of the predetermined product to a remote site while converting the carbonaceous feedstock into the said product using the onboard thermal conversion plant, the chemical reaction unit and the marine vessel's system.
  • FIG. 1 depicts a schematic of the present invention comprising a marine vessel, a first remote site and a second remote site.
  • the marine vessel performs intake of a carbonaceous feedstock from the first remote site into the vessel, and converts the feedstock into a syngas blend comprising CO and H 2 , and then converting syngas into a predetermined hydrocarbon product that is delivered and distributed to the second remote site.
  • FIG. 2 depicts a schematic of the present invention comprising a marine vessel, the vessel further comprising at least one thermal conversion plant, and at least one chemical reaction unit.
  • the thermal conversion plant converts the carbonaceous feedstock into a syngas blend comprising CO and H 2 ; the chemical reaction unit converts the syngas into a predetermined hydrocarbon product.
  • a marine vessel (2) performs intake and loading of a carbonaceous feedstock (A), from a first remote site (1 ).
  • the first remote site (1 ) may be a land-based terrestrial facility, or a second marine vessel, or an offshore platform, or a floating terminal platform.
  • the vessel (2) will also simultaneously convert the carbonaceous feedstock (A) into a hydrocarbon product (B), which is delivered and distributed to the second mote site (3).
  • the vessel (2) may conduct a second intake of additional carbonaceous feedstock (A) from the second remote site (3), to replenish the feedstock (A) that is consumed to produce the hydrocarbon product (B).
  • the marine vessel (2) may also conduct replenishment of the feedstock (A) while at the same time, distributing the hydrocarbon product (B) to the second remote site (3).
  • FIG. 2 converts a carbonaceous feedstock (A) FIG. 1 into a hydrocarbon product (B) FIG. 1 , by sending the feedstock (A) FIG. 1 into the thermal conversion plant (5) FIG. 2, and converting the feedstock (A) FIG. 1 into a syngas (7) FIG. 2, this syngas (7) FIG. 2, comprises CO, H 2 , and is an industrially valuable product by itself.
  • the syngas (7) FIG. 2 is passed into a chemical reaction unit (6) FIG. 2, to convert the syngas (7) FIG. 2 into the hydrocarbon product (B) FIG. 1.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Ocean & Marine Engineering (AREA)
  • Civil Engineering (AREA)
  • Architecture (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Selon la présente invention, la matière contenant du carbone est d'abord soumise à une conversion thermique pour donner un mélange de gaz de synthèse comprenant du monoxyde de carbone et de l'hydrogène (gaz de synthèse), la conversion thermique est chauffée au moyen d'un échangeur thermique, l'échangeur puisant en outre l'énergie thermique de la chaleur des déchets générée par le groupe motopropulseur d'un navire. Une énergie thermique supplémentaire peut être ajoutée à l'échangeur au moyen d'une source de chaleur secondaire. Le mélange de gaz de synthèse est ensuite soumis à une conversion chimique en un produit d'hydrocarbure ayant un nombre de carbones dans la plage variant entre C1 à C60. Le produit est isolé, recueilli et stocké à bord pour une livraison et une distribution ultérieures à au moins un site éloigné.
PCT/SG2007/000380 2006-11-07 2007-11-06 Groupe motopropulseur perfectionné de navire avec unité de gazéification de charbon et groupe motopropulseur à gaz de synthèse WO2008057051A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020097011854A KR20090107488A (ko) 2006-11-07 2007-11-06 석탄 가스화 유닛 및 합성가스 전력플랜트를 갖는 진보된 해양 선박 전력플랜트

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SG200607576-6 2006-11-07
SG200607576 2006-11-07

Publications (1)

Publication Number Publication Date
WO2008057051A1 true WO2008057051A1 (fr) 2008-05-15

Family

ID=39364776

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SG2007/000380 WO2008057051A1 (fr) 2006-11-07 2007-11-06 Groupe motopropulseur perfectionné de navire avec unité de gazéification de charbon et groupe motopropulseur à gaz de synthèse

Country Status (2)

Country Link
KR (1) KR20090107488A (fr)
WO (1) WO2008057051A1 (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009108132A2 (fr) * 2008-02-29 2009-09-03 How Kiap Gueh Synthèse et production d'hydrocarbures à bord de vaisseau maritime à partir d'une charge d'alimentation variée
WO2009108130A2 (fr) * 2008-02-29 2009-09-03 How Kiap Gueh Synthèse d'hydrocarbure et production à bord d'un système marin au moyen de matières premières diverses
WO2013183036A2 (fr) * 2012-06-08 2013-12-12 How Kiap Gueh Système réacteur de gazéification de masse fondue
WO2014064648A2 (fr) * 2012-10-25 2014-05-01 How Kiap Gueh Dispositifs et procédés de gazéification
WO2014115094A1 (fr) * 2013-01-23 2014-07-31 How Kiap Gueh Gazéificateur pour la génération de gaz de synthèse
WO2014163586A1 (fr) * 2013-04-03 2014-10-09 How Kiap Gueh Gazéificateur de métal fondu
EP3599342A1 (fr) * 2018-07-27 2020-01-29 Alphakat Holding International Ltd. Plateforme d'exploration pétrolière

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2541657A (en) * 1947-03-07 1951-02-13 Standard Oil Dev Co Method of making commercial mixtures of hydrogen and carbon monoxide
US2543005A (en) * 1947-03-18 1951-02-27 Socony Vacuum Oil Co Inc Method for conducting hightemperature conversions
US2931843A (en) * 1956-01-11 1960-04-05 Sinclair Refining Co Pyrolytic conversion of hydrocarbons employing a molten metal as a heat transfer medium
GB1475813A (en) * 1974-04-09 1977-06-10 Tapiola Ag Processing natural gas and products derived therefrom
US4134732A (en) * 1977-06-08 1979-01-16 Continental Oil Company Floating methanol plant
US4588850A (en) * 1983-08-26 1986-05-13 Huels Aktiengesellschaft Process for the production of acetylene and synthesis or reduction gas from coal in an electric arc process
US5177304A (en) * 1990-07-24 1993-01-05 Molten Metal Technology, Inc. Method and system for forming carbon dioxide from carbon-containing materials in a molten bath of immiscible metals
WO1997012118A1 (fr) * 1995-09-25 1997-04-03 Den Norske Stats Oljeselskap A/S Procede et dispositif de traitement d'un courant issu d'un puits d'un champ de petrole marin
WO2006092392A1 (fr) * 2005-03-01 2006-09-08 Shell Internationale Research Maatschappij B.V. Reformage de gtl pour des applications marines

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2541657A (en) * 1947-03-07 1951-02-13 Standard Oil Dev Co Method of making commercial mixtures of hydrogen and carbon monoxide
US2543005A (en) * 1947-03-18 1951-02-27 Socony Vacuum Oil Co Inc Method for conducting hightemperature conversions
US2931843A (en) * 1956-01-11 1960-04-05 Sinclair Refining Co Pyrolytic conversion of hydrocarbons employing a molten metal as a heat transfer medium
GB1475813A (en) * 1974-04-09 1977-06-10 Tapiola Ag Processing natural gas and products derived therefrom
US4134732A (en) * 1977-06-08 1979-01-16 Continental Oil Company Floating methanol plant
US4588850A (en) * 1983-08-26 1986-05-13 Huels Aktiengesellschaft Process for the production of acetylene and synthesis or reduction gas from coal in an electric arc process
US5177304A (en) * 1990-07-24 1993-01-05 Molten Metal Technology, Inc. Method and system for forming carbon dioxide from carbon-containing materials in a molten bath of immiscible metals
WO1997012118A1 (fr) * 1995-09-25 1997-04-03 Den Norske Stats Oljeselskap A/S Procede et dispositif de traitement d'un courant issu d'un puits d'un champ de petrole marin
WO2006092392A1 (fr) * 2005-03-01 2006-09-08 Shell Internationale Research Maatschappij B.V. Reformage de gtl pour des applications marines

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009108130A2 (fr) * 2008-02-29 2009-09-03 How Kiap Gueh Synthèse d'hydrocarbure et production à bord d'un système marin au moyen de matières premières diverses
WO2009108132A3 (fr) * 2008-02-29 2012-10-11 How Kiap Gueh Synthèse et production d'hydrocarbures à bord de vaisseau maritime à partir d'une charge d'alimentation variée
WO2009108130A3 (fr) * 2008-02-29 2012-10-11 How Kiap Gueh Synthèse d'hydrocarbure et production à bord d'un système marin au moyen de matières premières diverses
WO2009108132A2 (fr) * 2008-02-29 2009-09-03 How Kiap Gueh Synthèse et production d'hydrocarbures à bord de vaisseau maritime à partir d'une charge d'alimentation variée
US20150152344A1 (en) * 2012-06-08 2015-06-04 How Kiap Gueh Melt gasifier system
WO2013183036A2 (fr) * 2012-06-08 2013-12-12 How Kiap Gueh Système réacteur de gazéification de masse fondue
WO2013183036A3 (fr) * 2012-06-08 2014-02-20 How Kiap Gueh Système réacteur de gazéification de masse fondue
WO2014064648A2 (fr) * 2012-10-25 2014-05-01 How Kiap Gueh Dispositifs et procédés de gazéification
WO2014064648A3 (fr) * 2012-10-25 2014-07-17 How Kiap Gueh Dispositifs et procédés de gazéification
WO2014115094A1 (fr) * 2013-01-23 2014-07-31 How Kiap Gueh Gazéificateur pour la génération de gaz de synthèse
WO2014163586A1 (fr) * 2013-04-03 2014-10-09 How Kiap Gueh Gazéificateur de métal fondu
EP3599342A1 (fr) * 2018-07-27 2020-01-29 Alphakat Holding International Ltd. Plateforme d'exploration pétrolière
WO2020020481A1 (fr) * 2018-07-27 2020-01-30 Alphakat Holding International Ltd. Cypern Plate-forme pour la production d'huile

Also Published As

Publication number Publication date
KR20090107488A (ko) 2009-10-13

Similar Documents

Publication Publication Date Title
Olah et al. Beyond oil and gas: the methanol economy
Rafiee et al. Renewable hybridization of oil and gas supply chains
WO2008057051A1 (fr) Groupe motopropulseur perfectionné de navire avec unité de gazéification de charbon et groupe motopropulseur à gaz de synthèse
US6306917B1 (en) Processes for the production of hydrocarbons, power and carbon dioxide from carbon-containing materials
US6277894B1 (en) System and method for converting light hydrocarbons into heavier hydrocarbons with a plurality of synthesis gas subsystems
Socolow Fuels decarbonization and carbon sequestration: Report of a workshop
US20050232833A1 (en) Process for producing synthetic liquid hydrocarbon fuels
Shah Chemical energy from natural and synthetic gas
Ayvalı et al. The Position of Ammonia in Decarbonising Maritime Industry: An Overview and Perspectives: Part I: Technological advantages and the momentum towards ammonia-propelled shipping
KR20110116385A (ko) 해양에너지하이브리드시스템
US8431622B2 (en) Hydrocarbon synthesis and production onboard a marine system using varied feedstock
US8513316B2 (en) Hydrocarbon synthesis and production onboard a marine system using varied feedstock
WO2008057050A1 (fr) Procédé de production de méthane et d'hydrocarbures lourds depuis des vaisseaux maritimes équipés de systèmes d'irradiation aux ultraviolets
US8721750B2 (en) Hydrocarbon synthesis and production onboard a marine system using varied feedstock
EP0648174B1 (fr) Dispositif de production de produits petroliers en mer
WO2008057049A1 (fr) Vaisseau maritime comportant une installation à cycle combiné d'intégration et gazéification à base de plasma
JP2014088162A (ja) 発電プラントが搭載された浮遊式構造物及びその配置構造
US5935423A (en) Method for producing from a subterranean formation via a wellbore, transporting and converting a heavy crude oil into a distillate product stream
WO2008057052A1 (fr) Procédé de production de méthane et d'hydrocarbures lourds depuis des vaisseaux maritimes équipés d'une centrale nucléaire
WO2009108132A2 (fr) Synthèse et production d'hydrocarbures à bord de vaisseau maritime à partir d'une charge d'alimentation variée
WO2009108130A2 (fr) Synthèse d'hydrocarbure et production à bord d'un système marin au moyen de matières premières diverses
Lavate et al. Application of hydrogen in various sectors
Elgohary et al. The future role of natural gas in Saudi Arabia
Alkan Hydrogen Production and Bunkering from Offshore Wind Power Plants for Green and Sustainable Shipping
Steverson et al. Study concerning the utilization of the ocean spreading center environment for the conversion of biomass to a liquid fuel.(Includes Appendix A: hydrothermal petroleum genesis).[Supercritical water]

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07835535

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 1097/MUMNP/2009

Country of ref document: IN

Ref document number: 1020097011854

Country of ref document: KR

122 Ep: pct application non-entry in european phase

Ref document number: 07835535

Country of ref document: EP

Kind code of ref document: A1