WO2008057052A1 - Method of producing methane and heavy hydrocarbons from marine vessels equipped with nuclear powerplant - Google Patents

Method of producing methane and heavy hydrocarbons from marine vessels equipped with nuclear powerplant Download PDF

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Publication number
WO2008057052A1
WO2008057052A1 PCT/SG2007/000381 SG2007000381W WO2008057052A1 WO 2008057052 A1 WO2008057052 A1 WO 2008057052A1 SG 2007000381 W SG2007000381 W SG 2007000381W WO 2008057052 A1 WO2008057052 A1 WO 2008057052A1
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Prior art keywords
vessel
onboard
product
feedstock
marine vessel
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PCT/SG2007/000381
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French (fr)
Inventor
How Kiap Gueh
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How Kiap Gueh
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Application filed by How Kiap Gueh filed Critical How Kiap Gueh
Priority to KR1020097011852A priority Critical patent/KR20090107487A/en
Publication of WO2008057052A1 publication Critical patent/WO2008057052A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63BSHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B35/00Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for
    • B63B35/44Floating buildings, stores, drilling platforms, or workshops, e.g. carrying water-oil separating devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63HMARINE PROPULSION OR STEERING
    • B63H21/00Use of propulsion power plant or units on vessels
    • B63H21/18Use of propulsion power plant or units on vessels the vessels being powered by nuclear energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63JAUXILIARIES ON VESSELS
    • B63J99/00Subject matter not provided for in other groups of this subclass
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T70/00Maritime or waterways transport
    • Y02T70/50Measures to reduce greenhouse gas emissions related to the propulsion system

Definitions

  • a feedstock material containing some carbon is first subjected to thermal conversion to yield a gas blend comprising carbon monoxide and hydrogen (syngas), thermal conversion is supplied heat by means of a heat exchanger, exchanger further deriving thermal energy from a nuclear powerplant installed onboard a maritime vessel.
  • 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 6O , the product is isolated, collected and stored onboard for subsequent delivery and distribution to at least one remote site.
  • 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 C 10 , or Cu to C 2O , C 2 i to C 30 , or C 31 to C 6 Q
  • carbon-based fuels comprising a carbon number of between C 1 to C 4 , or C 5 to C 10 , or C 11 to C 2 o > 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
  • the marine drive (sometimes called a marine drive) coupling the engine to the propeller shalf.
  • 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.
  • 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.
  • 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.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Ocean & Marine Engineering (AREA)
  • Structural Engineering (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Toxicology (AREA)
  • Physics & Mathematics (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

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 a nuclear powerplant installed onboard a maritime vessel. The syngas blend is then subjected to chemical conversion into a hydrocarbon product having a carbon number in the range of between C1to C60, the product is isolated, collected and stored onboard for subsequent delivery and distribution to at least one remote site.

Description

Method of producing methane and heavy hydrocarbons from marine vessels equipped with nuclear powerplant
FIELD OF THE INVENTION
A feedstock material containing some carbon is first subjected to thermal conversion to yield a gas blend comprising carbon monoxide and hydrogen (syngas), thermal conversion is supplied heat by means of a heat exchanger, exchanger further deriving thermal energy from a nuclear powerplant installed onboard a maritime vessel. The syngas blend is then subjected to chemical conversion into a hydrocarbon product having a carbon number in the range of between C1 to C6O, the product is isolated, collected and stored onboard for subsequent delivery and distribution to at least one remote site.
PRIOR ART
US Patent: 4568522, Grumman Aerospace Corporation
BACKGROUND OF THE INVENTION
Currently, there is an unprecedented global demand for energy for industrial and economic development in several high growth regions of the world, and this demand has exceeded in many instances the total capacity of production of fossil-derived energy sources including crude, natural gas, and coal.
When alternative energy sources are factored into the energy supply/demand equilibrium, that is, nuclear, biomass, wind, solar, geothermal and hydro derived energy pools, it is still possible that demand exceeds production capacity. Fossil energy sources are now increasingly explored and mined in far-flung regions that is substantially further away from its demand markets, and in some circumstances, these energy sources are discovered in regions where overall operating environments may be difficult. In the field of natural gas exploration and development, substantial technology has been developed for gas liquefaction to convert natural gas into denser liquefied natural gas (LNG), or directly into hydrocarbons that is easier to transport using marine vessels.
These 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.
While the energy environment remains competitive and at times challenging, great potential can be found in still unexplored areas of the world include the Arctic/polar regions where undiscovered oil and gas reserves are estimated at 25% of total world supplies. Significant developments have also been made in the areas of tar sands and shale oil recovery to yield syncrude (synthetic crude).
Additionally, a gradual realization of an apparent acceleration of rising temperatures in almost every major part of the world have convinced many that the continued use and subsequent pollution of heat trapping gases such as carbon dioxide (CO2) cannot be reasonably sustained without dramatic implementation of technologies in the area of environmental regulation, emissions control, carbon sequestration/storage, and simply using fuels that are derived from renewable resources.
It is now estimated that a small elevation in global median temperatures can trigger varying amounts of flooding and sea level readjustments especially to coastal regions, and with large number of urban population centers also located at these places, along with their industrial infrastructure including power generation, transport, factories and manufacturing plants, this presents a potentially massive shift in locating these critical facets of the industrialized states to locations where the mentioned effects are less pronounced.
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. In addition to ships that either perform transportation of energy, there are vessels that can drill and extract energy, and further "production" vessels that can convert the extracted energy such as natural gas, into denser or more suitable forms, such as methanol, LNG, etc.
DEFINITION OF TERMS
For purposes of this specification and claims the following shall mean:
Marine vessel or ship or vessel
Refers to any floatation structure, vehicle, platform, and/or offshore platform. Could be operated in seawater, freshwater, or both. Usually referred to as 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
Refers to any device or system in which a flowing gas is passed through an electric arc, producing plasma. 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).
Gasification or pyrolysis
Refers to any thermal heating action or process acting on a material to yield gas blend containing elements originally present in the material prior to thermal heating action. In materials containing carbon and moisture, carbon monoxide and hydrogen is produced from this thermal heating action. This gas mixture of carbon monoxide (CO), hydrogen (H2) (along with other gases such as carbon dioxide etc.) is commonly called "Syngas". Generally, a carbonaceous material/feedstock can be converted by thermal means into a syngas blend. Gasification/pyrolysis can be interchangeably used to describe the process of converting the feedstock into Syngas.
Plasma gasification or plasma pyrolysis
Refers to any thermal heating action performed by a plasma producing device, or plasma producing apparatus, or plasma system (see above), on a material (or feedstock) to yield Syngas.
Carbonaceous feedstock or feedstock
Refers to any material containing some carbon. 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. Biomass, municipal waste, municipal solid waste (MSW), 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 sands, shale oil, peat, natural gas, petroleum, crude oil, oil wax, sewage, grass, agriculture derived waste, animal derived waste, are all considered as part of this definition of carbonaceous feedstock.
Hydrocarbon, or hydrocarbon product
Refers to a hydrocarbon product comprising a carbon number of between C1 to C4, or C5 to C10, or Cu to C2O, C2i to C30, or C31 to C6Q, further includes carbon-based fuels comprising a carbon number of between C1 to C4, or C5 to C10, or C11 to C2o> C21 to C30, or C31 to C6o, further includes gasoline, diesel, kerosene, methane, ethane, propane, butane, synthetic natural gas, methanol, light olefins, oxo-alcohols, ethanol.
Syngas or syn-gas or synthetic gas
Refers to any gas blend comprising of carbon monoxide (CO) and hydrogen (H2), and may further contain some portion of carbon dioxide (CO2) and other elements. 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.
Electrolysis
Refers to any device or system that can split water, seawater or any liquid or fluid or vapor phase gas mixture into component elements. Method of splitting into component elements may be electric, electrochemical, thermal or a combination.
Electric power or electric current
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.
Vessel powerplant
Refers to the prime mover device or system or engine of the vessel (marine 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. For marine vessels without a propeller driven propulsion, the marine drive would be the interface wherein energy generated from the powerplant is converted into propulsion for the vessel.
Powerplant
Refers to any power generating device or system. The device or system may produce mechanical power, or electric power, or both, depending on the type of powerplant. Includes reciprocating piston engines, gas turbines, steam turbines, auxiliary generator units, fuel cells, a battery system, rotary engines, combustion boiler that is coupled with an energy conversion apparatus (such as a steam turbine).
Induction heating apparatus/electric induction heat furnace
Refers to 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.
Thermal conversion plant
Refers to a system that is equipped onboard a marine vessel to perform the conversion of a carbonaceous feedstock into a Syngas blend comprising CO and H2, 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.
Chemical reaction unit/chemical reaction plant
Refers to a system that is equipped onboard a marine vessel to perform the conversion, or forming of a predetermined hydrocarbon product from a Syngas blend. 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. BRIEF DESCRIPTION OF THE DRAWINGS
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 H2, 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 H2; the chemical reaction unit converts the syngas into a predetermined hydrocarbon product.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
With reference to FIG. 1 , 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. Once the feedstock (A) is completely and satisfactorily loaded onto the vessel (2), it begins the journey to a designated second remote site (3). 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). Additionally, 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).
With reference to FIG. 1 and FIG. 2, a marine vessel (4) 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, H2, 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.
Modifications within the spirit and scope of the invention may readily be effected by persons skilled in the art. It is to be understood, therefore, that this invention is not limited to the particular embodiments described by way of example hereinabove.

Claims

Claims
1. A hydrocarbon product manufactured onboard a marine vessel and distributed to a plurality of remote sites, the process of manufacture and distribution comprising: A marine vessel performing intake of a predetermined carbonaceous feedstock from a first remote site, and converting feedstock into a syngas blend comprising CO and H2 using an onboard thermal conversion plant, and passing syngas blend into an onboard chemical reaction unit to form a predetermined hydrocarbon product, and vessel delivering the product from vessel to a second remote site.
2. The process of claim 1 , marine vessel comprising at least one nuclear powerplant, and
(a) thermal conversion plant is operationally connected to the nuclear powerplant,
(b) nuclear powerplant supplying energy to the thermal conversion plant to perform conversion of feedstock into syngas.
3. A hydrocarbon product manufactured onboard a marine vessel and distributed to a plurality of remote sites, the method of manufacture and distribution comprising: A marine vessel performing intake of a predetermined carbonaceous feedstock from a first remote site, and converting feedstock into a syngas blend comprising CO and H2 using an onboard thermal conversion plant, and passing syngas blend into an onboard chemical reaction unit to form a predetermined hydrocarbon product, and vessel delivering the product from vessel to a second remote site.
4. The method of claim 3, marine vessel comprising at least one nuclear powerplant, and
(a) thermal conversion plant is operationally connected to the nuclear powerplant,
(b) nuclear powerplant supplying energy to the thermal conversion plant to perform conversion of feedstock into Syngas.
5. A hydrocarbon product manufactured onboard a marine vessel and distributed to a plurality of remote sites, the process of manufacture and distribution comprising: A marine vessel performing intake of a predetermined liquid phase feedstock from a first remote site, and converting feedstock into an intermediate gas blend comprising CO2 and CH4 using an onboard anaerobic reactor system, and passing gas blend into an onboard gas treatment unit to isolate and collect CH4 product, and vessel delivering the CH4 product from vessel to a second remote site.
6. The process of claim 5, onboard gas treatment unit comprising a pressure swing absorption module, and
(a) said module isolating CH4 product from the gas blend,
(b) passing CH4 product into a storage system onboard marine vessel.
7. A hydrocarbon product manufactured onboard a marine vessel and distributed to a plurality of remote sites, the method of manufacture and distribution comprising: A marine vessel performing intake of a predetermined liquid phase feedstock from a first remote site, and converting feedstock into an intermediate gas blend comprising CO2 and CH4 using an onboard anaerobic reactor system, and passing gas blend into an onboard gas treatment unit to isolate and collect CH4 product, and vessel delivering the CH4 product from vessel to a second remote site.
8. The method of claim 7, onboard gas treatment unit comprising a pressure swing absorption module, and
(a) said module isolating CH4 product from the gas blend,
(b) passing CH4 product into a storage system onboard marine vessel.
9. A hydrocarbon oil product manufactured onboard a marine vessel and distributed to a plurality of remote sites, the process of manufacture and distribution comprising: A' marine vessel performing intake of a predetermined carbonaceous feedstock from a first remote site, and subjecting the feedstock to heat and pressurization in a reaction plant system, forming a hydrocarbon oil product, and vessel delivering the product from vessel to a second remote site.
10. The process of claim 13, reaction plant system performing the steps of,
(a) intake of the feedstock into a first reaction vessel,
(b) addition of water in the first reaction vessel, (c) pressurizing and heating the first reaction vessel for a predetermined time period to form a crude slurry,
(d) separating water from the slurry and subjecting slurry to thermal distillation,
(e) isolating oil product from distillation and storing product for subsequent delivery and distribution to second remote site.
PCT/SG2007/000381 2006-11-07 2007-11-06 Method of producing methane and heavy hydrocarbons from marine vessels equipped with nuclear powerplant WO2008057052A1 (en)

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Citations (7)

* 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
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
US4568522A (en) * 1982-09-13 1986-02-04 Grumman Aerospace Corporation Synfuel production ship
GB2276353A (en) * 1993-03-25 1994-09-28 Offshore Production Systems Li Floating methanol production complex
WO1997012118A1 (en) * 1995-09-25 1997-04-03 Den Norske Stats Oljeselskap A/S Method and system for the treatment of a well stream from an offshore oil field
US20040065614A1 (en) * 2002-10-08 2004-04-08 Gordon Andrew W. Mobile desalination plants and systems, and methods for producing desalinated water

Patent Citations (7)

* 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
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
US4568522A (en) * 1982-09-13 1986-02-04 Grumman Aerospace Corporation Synfuel production ship
GB2276353A (en) * 1993-03-25 1994-09-28 Offshore Production Systems Li Floating methanol production complex
WO1997012118A1 (en) * 1995-09-25 1997-04-03 Den Norske Stats Oljeselskap A/S Method and system for the treatment of a well stream from an offshore oil field
US20040065614A1 (en) * 2002-10-08 2004-04-08 Gordon Andrew W. Mobile desalination plants and systems, and methods for producing desalinated water

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SG163435A1 (en) 2010-08-30

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