CA2839107A1 - Lng export terminal - Google Patents

Lng export terminal Download PDF

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Publication number
CA2839107A1
CA2839107A1 CA2839107A CA2839107A CA2839107A1 CA 2839107 A1 CA2839107 A1 CA 2839107A1 CA 2839107 A CA2839107 A CA 2839107A CA 2839107 A CA2839107 A CA 2839107A CA 2839107 A1 CA2839107 A1 CA 2839107A1
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CA
Canada
Prior art keywords
lng
vessel
carrier
natural gas
export terminal
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.)
Granted
Application number
CA2839107A
Other languages
French (fr)
Other versions
CA2839107C (en
Inventor
Michael Wyllie
Theodorus Johannes Bernardus Brinkel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Single Buoy Moorings Inc
Original Assignee
SBM Schiedam BV
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 SBM Schiedam BV filed Critical SBM Schiedam BV
Priority to CA2839107A priority Critical patent/CA2839107C/en
Priority to CA2842621A priority patent/CA2842621A1/en
Publication of CA2839107A1 publication Critical patent/CA2839107A1/en
Application granted granted Critical
Publication of CA2839107C publication Critical patent/CA2839107C/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B25/00—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby
    • B63B25/02—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods
    • B63B25/08—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid
    • B63B25/12—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid closed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B27/00—Arrangement of ship-based loading or unloading equipment for cargo or passengers
    • B63B27/24—Arrangement of ship-based loading or unloading equipment for cargo or passengers of pipe-lines
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B27/00—Arrangement of ship-based loading or unloading equipment for cargo or passengers
    • B63B27/30—Arrangement of ship-based loading or unloading equipment for transfer at sea between ships or between ships and off-shore structures
    • B63B27/34—Arrangement of ship-based loading or unloading equipment for transfer at sea between ships or between ships and off-shore structures using pipe-lines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
    • F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
    • F25J1/0277—Offshore use, e.g. during shipping
    • F25J1/0278—Unit being stationary, e.g. on floating barge or fixed platform
    • 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
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B71/00—Designing vessels; Predicting their performance
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/60—Details about pipelines, i.e. network, for feed or product distribution

Abstract

A near shore liquefied natural gas (LNG) export terminal includes an LNG storage unit, a jetty and a converted hydrocarbon carrier-vessel moored against the jetty. The carrier-vessel includes a hull, at least one hydrocarbon storage tank and is provided with a natural gas processing system for liquefying natural gas. Onshore produced natural gas is supplied through a first pipeline to the natural gas processing plant on the carrier-vessel and the LNG produced by the natural gas processing system is transferred from the carrier-vessel to the LNG storage unit via a second pipeline suitable for the transfer of cryogenic fluids.

Description

LNG export terminal Field of the invention The present invention relates to an near shore LNG export terminal, comprising a floating natural gas processing system and an LNG storage unit.
Background Such terminals have been described in the prior art. US2940268, for example, teaches to liquefy of natural gas in a barge mounted liquefaction plant and to subsequent discharge the liquefied natural gas into suitably insulated storage tanks, preferably installed on a tank carrying vessel. The barges described in US2940268 are often custom made in specialized wharfs and they mostly lack proper propulsion to reach their operational destination, so that they need to be towed or transported, sometimes over large distances. The risk of damage to the barge during the journey to the operational destination is clear and present. Furthermore, the facilities provided on the barge are limited and it may be necessary to provide extensive facilities onshore. Providing facilities onshore is difficult and/or requires important investments on some operational sites.
Summary of the invention It is an object of the present invention is to provide an improved liquefied natural gas (LNG) export terminal which reduces the disadvantages and limitations of the LNG export terminals, known from the prior art.
Thereto, the near shore liquefied natural gas (LNG) export terminal comprising an LNG storage unit, a jetty and a converted hydrocarbon carrier-vessel moored against the jetty, the carrier-vessel comprising a hull, at least one hydrocarbon storage tank and being provided with a natural gas processing system for liquefying natural gas, wherein onshore produced natural gas is supplied through a first pipeline to the natural gas processing plant on the converted hydrocarbon carrier-vessel, the converted hydrocarbon carrier vessel is arranged to receive the onshore produced natural gas and to transfer the LNG produced by the natural gas processing
2 system from the carrier-vessel to the LNG storage unit via a second pipeline suitable for the transfer of cryogenic fluids.
The inventors have observed that instead of using a flat-top barge, as described in the prior art, the use of a converted hydrocarbon carrier-vessel as a platform for the natural gas processing system for liquefying natural gas offers the advantage that some functionalities of the converted hydrocarbon carrier-vessel can be re-used and have to be newly built on a flat-top barge, such as, but not limited to, a deckhouse for operational people on board, possibly only during dayshift, going home after work, supporting facilities for people on-board (drinking water, sewage treatment),safety systems in the accommodation area, boiler (to provide process heat and for start-up), and emergency power supply.
Other functionalities such as propulsion, for sailing on own power from the conversion/assembly yard to the final operational destination, are available as well.
Within the frame-work of the present invention, it will be appreciated that the term "jetty-moored" encompasses also quay-moored or any other near-shore mooring.
The liquefaction process in the natural gas processing system involves removal of certain components, such as dust, acid gases, helium, water, and heavy hydrocarbons, that could cause difficulty downstream. The natural gas is then condensed into a liquid at close to atmospheric pressure (maximum transport pressure set at around 25 kPa (4 psi)) by cooling it to approximately ¨162 C (-260 F).
According to an embodiment of the present invention, the LNG storage unit comprises one or a plurality of onshore LNG storage tanks.
According to an embodiment of the present invention, the onshore LNG
storage tank is connectable through a further pipeline to an LNG shuttle tanker.
According to an embodiment of the present invention, the LNG storage unit comprises an LNG storage tanker having storage tanks for containing LNG.
According to an embodiment of the present invention, the storage tanks are spherical tanks.
According to an embodiment of the present invention, the LNG storage tanks are membrane tanks.
According to an embodiment of the present invention, the LNG storage tanker is connectable through a further pipeline to a further LNG shuttle tanker.
3 According to an embodiment of the present invention, the converted hydrocarbon carrier-vessel further comprises one or more facilities selected from a group comprising living quarters, maintenance facilities, safety systems, emergency escape and evacuation systems, logistic systems and power generation systems.
According to an embodiment of the present invention, the converted hydrocarbon carrier-vessel is a converted oil tanker.
According to an embodiment of the present invention, the converted oil tanker is a converted very large crude carrier (VLCC).
According to an embodiment of the present invention, the converted hydrocarbon carrier-vessel is a converted LNG carrier.
According to an embodiment of the present invention, the second and further pipelines are cryogenic hoses.
Advantageous embodiments are further defined by the dependent claims.
Brief description of drawings Presently preferred embodiments are described below in conjunction with the appended drawing figures, wherein like reference numerals refer to like elements in the various figures, and wherein:
Figure 1 illustrates an LNG export terminal with a converted hydrocarbon carrier and an onshore placed LNG storage tank;
Figure 2 illustrates the LNG export terminal of figure 1 with an LNG shuttle carrier moored against the jetty and receiving LNG from the onshore LNG
storage tank;
Figure 3 illustrates an alternative LNG export terminal with a converted hydrocarbon carrier and an moored LNG storage vessel for storage of the produced LNG;
Figure 4 illustrates the alternative LNG export terminal of figure 3 with a moored LNG shuttle carrier receiving the produced and stored LNG from the LNG
storage tanker;
Figure 5 schematically shows an LNG export terminal according to a further embodiment.
4 Detailed description of embodiments The present invention will be described with respect to particular embodiments and with reference to certain drawings but the invention is not limited thereto. The drawings described are only schematic and are non-limiting. In the drawings, the size of some of the elements may be exaggerated and not drawn on scale for illustrative purposes.
Furthermore, the terms first, second, third and the like in the description are used for distinguishing between similar elements and not necessarily for describing a sequential or chronological order. The terms are interchangeable under appropriate circumstances and the embodiments of the invention can operate in other sequences than described or illustrated herein.
Moreover, the terms top, bottom, over, under and the like in the description are used for descriptive purposes and not necessarily for describing relative positions.
The terms so used are interchangeable under appropriate circumstances and the embodiments of the invention described herein can operate in other orientations than described or illustrated herein.
The term "comprising" should not be interpreted as being restricted to the means listed thereafter; it does not exclude other elements or steps. It needs to be interpreted as specifying the presence of the stated features, integers, steps or components as referred to, but does not preclude the presence or addition of one or more other features, integers, steps or components, or groups thereof. Thus, the scope of the expression "a device comprising means A and B" should not be limited to devices consisting of only components A and B. It means that with respect to the present description, the only relevant components of the device are A and B.
Figure 1 schematically shows an LNG export terminal 1 with a converted hydrocarbon carrier-vessel 100 and an onshore placed LNG storage tank 30 in accordance with an embodiment of the present invention.
The LNG export terminal 50 comprises a converted hydrocarbon carrier-vessel 100, an LNG storage unit 20 and a jetty 10.
The converted hydrocarbon carrier-vessel 100 is arranged in coastal water 1 of a sea or a lake and is moored against the jetty 10, relatively close to shore 15.

The converted hydrocarbon carrier-vessel 100 comprises a hull, and is provided with a natural gas processing system (liquefaction system) 101 for liquefying natural gas.
The liquefaction system 101 typically comprises at least one hydrocarbon
5 storage tank 102.
From a source 20, onshore produced natural gas is supplied through a first pipeline 25 to an input 21 of the natural gas processing plant 101, 102 on the converted hydrocarbon carrier-vessel 100.
The converted hydrocarbon carrier-vessel 100 is arranged to receive the onshore produced natural gas, to produce LNG in the liquefaction system 101, and to transfer from an output 31 of the liquefaction system, the LNG product to the onshore LNG storage unit 30 via a second pipeline 35 suitable for the transfer of cryogenic fluids.
In an embodiment, both the first and second pipelines 25, 35, run along the jetty between the converted hydrocarbon carrier-vessel 100 and the shore 15.
It is noted that alternatively the converted hydrocarbon carrier-vessel could be spread-moored or turret-moored.
In an embodiment the converted hydrocarbon carrier-vessel is either a converted oil tanker, or a converted very large crude carrier (VLCC) or a converted LNG carrier.
In an embodiment, the first and/or second pipelines 25, 35 may be embodied as cryogenic hoses.
Further, as schematically indicated, the converted hydrocarbon carrier-vessel 100 may comprise facilities such as one or more of living quarters, maintenance facilities, safety systems, emergency escape and evacuation systems, logistic systems and one or more power generation systems.
Figure 2 schematically shows the LNG export terminal 50 in accordance with a further embodiment.
In this embodiment the LNG export terminal is configured to receive an LNG
shuttle tanker or vessel 200 that functions as an offshore LNG storage unit and LNG
carrier.
6 The LNG shuttle tanker 200 is arranged with LNG storage tanks 250 for storing LNG.
The LNG export terminal's jetty 10 is configured for mooring of the LNG
shuttle tanker 200. Additionally, the second pipeline 25 is arranged with an LNG
product outlet 32 that can be coupled to an input of the LNG shuttle tanker 200, in such a way that the LNG shuttle tanker can receive LNG from the onshore LNG
storage tank 30.
In a further embodiment, the second pipeline 35 may be configured to allow direct transfer of LNG from output 31 of the converted hydrocarbon carrier-vessel 100 to outlet 35 coupled to the LNG shuttle tanker 200.
Optionally, the converted hydrocarbon carrier-vessel 100 may be configured to have the LNG shuttle tanker 200 mooring along the hull.
Figure 3 schematically shows an LNG export terminal 60 in an alternative embodiment.
In this embodiment, the onshore LNG storage tank 30 is omitted and replaced by a first LNG storage vessel 200 that functions as an LNG storage unit.
The first LNG storage vessel 200 may be an LNG shuttle tanker or an LNG
storage tanker, and is arranged with LNG storage tanks 250 for storing LNG.
In this embodiment, the converted hydrocarbon carrier-vessel 100 is moored against the jetty 10 and has the capability to have the first LNG storage vessel 200 mooring along its free side of the hull.
Alternatively, the first LNG storage vessel 200 may be moored against the jetty 10 with the converted hydrocarbon carrier-vessel 100 mooring along a free side of the hull of the first LNG storage vessel 200.
In a further alternative, the converted hydrocarbon carrier-vessel 100 and the first LNG storage vessel 200 are arranged lengthwise in line (or in tandem), each moored against the same side of the jetty 10.
From the source 20, onshore produced natural gas is supplied through the first pipeline 25 to the input 21 of the natural gas processing plant 101, 102 on the converted hydrocarbon carrier-vessel 100.
The converted hydrocarbon carrier-vessel 100 is arranged to produce LNG in the liquefaction system 101, 102 and to transfer from the liquefaction system, the
7 LNG product directly to the LNG storage tanks 250 on the first LNG storage vessel 200 via a second pipeline 33.
Additionally, the first LNG storage vessel 200 is equipped with a further pipeline 34 is arranged with an LNG product outlet 36 that can be coupled to an input of a further LNG shuttle vessel (not shown) that can moor along the jetty 10.
In this manner, the first LNG shuttle carrier vessel can function as an LNG storage tank, while the further LNG shuttle vessel is used a carrier for the LNG product.
This can be advantageous in locations where it is difficult to construct an onshore LNG

storage.
Figure 4 illustrates the alternative LNG export terminal 60 of figure 3. A
further LNG shuttle vessel 300 is moored at the jetty 10. The further LNG
shuttle vessel 300 comprises LNG storage tanks 350 for storing LNG.
During loading, the LNG storage system on the further LNG shuttle vessel 300 is coupled via the further pipeline 36 with the first LNG shuttle vessel 200 that functions as LNG storage.
In this manner the moored further LNG shuttle vessel 300 is arranged to receive the produced and/or stored LNG either from the liquefaction system 101, 102 converted hydrocarbon carrier-vessel 100 directly or from the LNG storage on the first LNG shuttle vessel 200.
Figure 5 schematically shows an LNG export terminal according to a further embodiment. In this embodiment, the LNG export terminal 50; 60 is arranged to receive additional LNG shuttle tankers 200 at the jetty 10 at a same time. The LNG
shuttle tankers can be moored in line against the jetty.
The pipeline(s) 35 of the LNG export terminal handling the produced LNG
are adapted with additional outlets to allow multiple LNG shuttle tankers to be served at the same time. In dependence on the specific embodiment, the tankers can be loaded from either the onshore LNG storage 30, the LNG storage vessel 200 or directly from the liquefaction system 101, 102 onboard the converted hydrocarbon carrier-vessel 100 or in a combination thereof.
According to the invention, the pipelines 25; 35 as described above may be pipelines suitable for cryogenic substances or may be cryogenic hoses. Instead of a jetty 10, the LNG export terminal may comprise a quay or a breakwater type or a
8 mooring arrangement with dolphin type mooring construction for mooring the converted hydrocarbon carrier vessel or in some embodiments, the first LNG
storage vessel.
The foregoing description details certain embodiments of the invention. It will be appreciated, however, that no matter how detailed the foregoing appears in text, the invention may be practiced in many ways. It should be noted that the use of particular terminology when describing certain features or aspects of the invention should not be taken to imply that the terminology is being re-defined herein to be restricted to including any specific characteristics of the features or aspects of the invention with which that terminology is associated.
While the above detailed description has shown, described, and pointed out novel features of the invention as applied to various embodiments, it will be understood that various modifications in the form and details of the device or process illustrated may be made by those skilled in the technology without departing from the spirit of the invention. The scope of the invention is indicated by the appended claims rather than by the foregoing description. All modifications that come within the meaning and range of equivalency of the claims are to be embraced within their scope.

Claims (12)

9
1. Near shore liquefied natural gas (LNG) export terminal comprising an LNG
storage unit, a jetty and a converted hydrocarbon carrier-vessel moored against the jetty, the carrier-vessel comprising a hull, at least one hydrocarbon storage tank and is provided with a natural gas processing system for liquefying natural gas, wherein onshore produced natural gas is supplied through a first pipeline to the natural gas processing plant on the converted hydrocarbon carrier-vessel, the converted hydrocarbon carrier vessel is arranged to receive the onshore produced natural gas and to transfer the LNG
produced by the natural gas processing system from the carrier-vessel to the LNG storage unit via a second pipeline suitable for the transfer of cryogenic fluids.
2. LNG export terminal according to claim 1, wherein the LNG storage unit comprises one or more LNG storage tanks that are placed onshore.
3. LNG export terminal according to claim 2, wherein the onshore placed LNG
storage tank is connected via a cryogenic pipeline to the tanks of a LNG
shuttle tanker that is temporary moored against the jetty.
4. LNG export terminal according to claim 1, wherein the LNG storage unit is an LNG storage tanker having storage tanks for the produced LNG and which is moored directly against the jetty or against the converted hydrocarbon carrier-vessel.
5. LNG export terminal according to claim 4, wherein the storage tanks are spherical tanks.
6. LNG export terminal according to claim 4, wherein the LNG storage tanks are membrane tanks.
7. LNG export terminal according to claim 4, wherein the LNG storage tanker is connectable through a further cryogenic pipeline or hose to a LNG shuttle tanker that is temporary moored against the jetty, the LNG storage tanker or the converted hydrocarbon carrier-vessel.
8. LNG export terminal according to claim 1, wherein the converted hydrocarbon carrier-vessel further comprises one or more of living quarters, maintenance facilities, safety systems, emergency escape and evacuation systems, logistic systems and power generation.
9. LNG export terminal according to claim 1, wherein the converted hydrocarbon carrier-vessel is a converted oil tanker.
10. LNG export terminal according to claim 9, wherein the converted oil tanker is a converted very large crude carrier (VLCC).
11. LNG export terminal according to claim 1, wherein the converted hydrocarbon carrier-vessel is a converted LNG carrier.
12. LNG export terminal according to claim 1, wherein the second and further pipelines are cryogenic hoses.
CA2839107A 2014-01-13 2014-01-13 Lng export terminal Active CA2839107C (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CA2839107A CA2839107C (en) 2014-01-13 2014-01-13 Lng export terminal
CA2842621A CA2842621A1 (en) 2014-01-13 2014-02-12 Lng export terminal with a twin-hull fso

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA2839107A CA2839107C (en) 2014-01-13 2014-01-13 Lng export terminal

Publications (2)

Publication Number Publication Date
CA2839107A1 true CA2839107A1 (en) 2015-07-13
CA2839107C CA2839107C (en) 2021-01-26

Family

ID=53546299

Family Applications (2)

Application Number Title Priority Date Filing Date
CA2839107A Active CA2839107C (en) 2014-01-13 2014-01-13 Lng export terminal
CA2842621A Abandoned CA2842621A1 (en) 2014-01-13 2014-02-12 Lng export terminal with a twin-hull fso

Family Applications After (1)

Application Number Title Priority Date Filing Date
CA2842621A Abandoned CA2842621A1 (en) 2014-01-13 2014-02-12 Lng export terminal with a twin-hull fso

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Also Published As

Publication number Publication date
CA2839107C (en) 2021-01-26
CA2842621A1 (en) 2015-07-13

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