EP2672213B1 - Gasification device for low-temperature liquefied gas - Google Patents
Gasification device for low-temperature liquefied gas Download PDFInfo
- Publication number
- EP2672213B1 EP2672213B1 EP11860385.1A EP11860385A EP2672213B1 EP 2672213 B1 EP2672213 B1 EP 2672213B1 EP 11860385 A EP11860385 A EP 11860385A EP 2672213 B1 EP2672213 B1 EP 2672213B1
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- European Patent Office
- Prior art keywords
- vaporizing
- region
- heat
- inlet
- inter
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- 238000002309 gasification Methods 0.000 title 1
- 230000008016 vaporization Effects 0.000 claims description 165
- 239000007788 liquid Substances 0.000 claims description 72
- 239000006200 vaporizer Substances 0.000 claims description 62
- 238000005192 partition Methods 0.000 claims description 8
- 239000013535 sea water Substances 0.000 description 68
- 239000003949 liquefied natural gas Substances 0.000 description 66
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 22
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Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
- F28D3/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits with tubular conduits
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
- F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
- F28D3/04—Distributing arrangements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D5/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
- F28D5/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/14—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by endowing the walls of conduits with zones of different degrees of conduction of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
- F28F9/0273—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple holes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/03—Mixtures
- F17C2221/032—Hydrocarbons
- F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/03—Mixtures
- F17C2221/032—Hydrocarbons
- F17C2221/035—Propane butane, e.g. LPG, GPL
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
- F17C2225/0107—Single phase
- F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0309—Heat exchange with the fluid by heating using another fluid
- F17C2227/0316—Water heating
- F17C2227/0318—Water heating using seawater
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
- F17C2227/0393—Localisation of heat exchange separate using a vaporiser
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/05—Regasification
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2270/00—Thermal insulation; Thermal decoupling
Definitions
- the present invention relates to a vaporizer for vaporizing a cryogenic liquid, such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN 2 ), by means of heat exchange with a heat medium such as seawater.
- a cryogenic liquid such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN 2 )
- LNG liquefied natural gas
- LPG liquefied petroleum gas
- LN 2 liquid nitrogen
- this vaporizer comprises a vaporizing tube panel 102 extending along a specific vertical plane, and a seawater supply section 104 for supplying seawater to the vaporizing tube panel 102.
- the vaporizing tube panel 102 comprises a plurality of vaporizing tubes (heat transfer tubes) 106, and an inter-vaporizing tube distribution pipe (inlet-side header) 108.
- the seawater supply section 104 is designed to supply seawater from an upper end of the vaporizing tube panel 102 to allow the seawater to flow down along a surface of the vaporizing tube panel 102.
- Each of the vaporizing tubes 106 is disposed to extend in a vertical direction to allow a liquefied natural gas (cryogenic liquid) to flow therethrough so as to cause a heat exchange with an external medium, thereby vaporizing the liquefied natural gas.
- the plurality of vaporizing tubes 106 comprised in the vaporizing tube panel 102 are arranged on the specific vertical plane and side-by-side in a horizontal direction to have mutually parallel postures.
- the inter-vaporizing tube distribution pipe 108 is designed to distribute liquefied natural gas to the respective vaporizing tubes 106 comprised in the vaporizing tube panel 102.
- the inter-vaporizing tube distribution pipe 108 is disposed to extend in the horizontal direction and connected to respective lower ends of the vaporizing tubes 106 comprised in the vaporizing tube panel 102.
- the inter-vaporizing tube distribution pipe 108 distributes liquefied natural gas to the respective vaporizing tubes 106, and the distributed liquefied natural gas flows through each of the vaporizing tubes 106 upwardly.
- seawater supplied from the seawater supply section 104 flows down along and outside the vaporizing tubes 106.
- heat exchange is performed between the liquefied natural gas and the seawater, through a tube wall of the vaporizing tube 106 separating an inside and an outside thereof. This allows the liquefied natural gas to be vaporized into natural gas (NG).
- NG natural gas
- a water protection cover 110 is disposed to cover an upper side of a first region a1 of the inter-vaporizing tube distribution pipe 108.
- the water protection cover 110 is designed to prevent seawater from directly hitting against the first region a1 of the inter-vaporizing tube distribution pipe 108. This makes it possible to suppress a fluctuation in heat amount of liquefied natural gas (vaporized liquefied natural gas) when the vaporizer is operated at a low load under a condition that a temperature of seawater is relatively high.
- the vaporizer disclosed in the Patent Document 1 when a cryogenic liquid (liquefied natural gas) is vaporized, a difference in temperature occurs between an end (region a2 in FIG. 11 ) and a central portion (region a2 in FIG. 11 ) of the inter-vaporizing tube distribution pipe 108 in a longitudinal direction of the distribution pipe 108. If such a temperature difference occurs, the inter-vaporizing tube distribution pipe 108 is likely to undergo bending deformation, due to a difference in amount of thermal expansion/shrinkage in each of the vaporizing tubes 106 caused by the temperature difference. This results in the occurrence of warpage in the inter-vaporizing tube distribution pipe 108, and the occurrence of stress in a joining area between the inter-vaporizing tube distribution pipe 108 and each of the vaporizing tubes 106.
- a cryogenic liquid liquefied natural gas
- a temperature in a region located longitudinally outside a region a1 of the inter-vaporizing tube distribution pipe 108 where the plurality of vaporizing tubes 106 are arranged becomes greater than a temperature in the region a1. That is, in the inter-vaporizing tube distribution pipe 108, a temperature of a longitudinal end a2 becomes greater than a temperature of the region a1. This is based on the following reason.
- the water protection cover 110 can prevent the heat-exchanging liquid from directly hitting against the first region a1 of the inter-vaporizing tube distribution pipe 108.
- the water protection cover 110 covers only a region adjacent to the vaporizing tube 106 at the endmost position, in the horizontal direction.
- a (relatively high-temperature) heat-exchanging liquid subjected to no heat exchange with the cryogenic liquid also hits against the second region a2 of the inter-vaporizing tube distribution pipe 108.
- Patent Document 3 discloses a cryogenic liquid vaporizer having the features defined in the preambles of claims 1 and 6.
- Patent Documents 4 to 8 Other conventional vaporizers are known from Patent Documents 4 to 8.
- Patent Documents 4 to 7 suggest suppressing heat transfer from the heat-exchanging liquid to a region of the inter-vaporizing tube distribution tube where the vaporizing tubes are arranged.
- a cryogenic liquid vaporizer for vaporizing a cryogenic liquid, which comprises the features defined in claim 1.
- the heat-transfer suppressing section functions to suppress a heat transfer amount per unit area, from the heat-exchanging liquid to the second region.
- the heat-transfer suppressing section may be a heat insulating member surrounding the second region of the inter-vaporizing tube distribution pipe, wherein the heat insulating member has a heat conductivity less than a heat conductivity of the inter-vaporizing tube distribution pipe.
- This configuration makes it possible to suppress a heat transfer amount per unit area from the heat-exchanging liquid to the second region of the inter-vaporizing tube distribution pipe, as compared to a heat transfer amount per unit area from the heat-exchanging liquid to the first region of the inter-vaporizing tube distribution pipe, in an easy and reliable manner.
- the heat insulating member has given stretchability.
- This configuration makes it possible to prevent damage of the heat insulating member due to thermal expansion/shrinkage of the inter-vaporizing tube distribution pipe.
- the heat insulating member surrounding the inter-vaporizing tube distribution pipe has given stretchability.
- the heat insulating member can stretch or contract according to thermal expansion/shrinkage of the inter-vaporizing tube distribution pipe. This makes it possible to effectively prevent damage of the heat insulating member due to thermal expansion/shrinkage (particularly, thermal expansion/shrinkage in a radial direction) of the inter-vaporizing tube distribution pipe.
- the heat-transfer suppressing section may be a cover member which is disposed on an upper side of the second region of the inter-vaporizing tube distribution pipe, and formed in a shape capable of covering over the second region of the inter-vaporizing tube distribution pipe, in top plan view.
- This configuration can prevent the heat-exchanging liquid flowing down outside the vaporizing tube at the endmost position in a longitudinal direction of the inter-vaporizing tube distribution pipe (horizontal direction) and undergoing almost no heat exchange with the cryogenic liquid flowing through the vaporizing tube, from hitting against the second region of the inter-vaporizing tube distribution pipe. This makes it possible to prevent the occurrence of a temperature difference between the first region and the second region in the inter-vaporizing tube distribution pipe.
- the second region is a region between the partition wall and the vaporizing tube located on the side of the one end.
- a cryogenic liquid vaporizer for vaporizing a cryogenic liquid, which comprises the features defined in claim 6.
- the heat conductivity of the pipe wall in the second region of the inter-vaporizing tube distribution pipe is less than that of the pipe wall in the first region of the inter-vaporizing tube distribution pipe, so that, even when a heat-exchanging liquid having a temperature greater than that of the first region of the inter-vaporizing tube distribution pipe hits against the second region of the inter-vaporizing tube distribution pipe, it becomes possible to prevent the occurrence of a temperature difference between the cryogenic liquid flowing through the first region of the inter-vaporizing tube distribution pipe, and the cryogenic liquid flowing through the second region of the inter-vaporizing tube distribution pipe. This makes it possible to prevent bending deformation of the inter-vaporizing tube distribution pipe due to the above temperature difference.
- a cryogenic liquid vaporizer (hereinafter also referred to simply as “vaporizer”) according to this embodiment is a so-called open rack vaporize (ORV) for subjecting a supplied cryogenic liquid to heat exchange with an external heat-exchanging liquid to thereby vaporize the cryogenic liquid.
- the vaporizer according to this embodiment is designed to vaporize a liquefied natural gas (LNG).
- LNG liquefied natural gas
- the heat-exchanging liquid for use in this embodiment is seawater.
- the vaporizer comprises a plurality of (in this embodiment, two) vaporizing tube blocks 11, a distributing pipe 12, a collecting pipe 14, and a seawater supply section (liquid supply section) 30.
- the distributing pipe 12 is designed to distribute LNG to the respective vaporizing tube blocks 11.
- the collecting pipe 14 is designed to collect vaporized LNG (natural gas (NG)) from the vaporizing tube blocks 11.
- the seawater supply section 30 is designed to supply seawater to an upper portion of each of a plurality of aftermentioned vaporizing tube panels 16 to allow the seawater to flow down along a surface of the vaporizing tube panel 16.
- the number of the vaporizing tube blocks 11 to be provided in the vaporizer 10 is not limited to two or more, but may be one.
- Each of the vaporizing tube blocks 11 comprises a plurality of (in this embodiment, five) vaporizing tube panels 16, an inlet-side manifold 17, and an outlet-side manifold 19.
- the number of the vaporizing tube panels 16 to be comprised in one of the vaporizing tube blocks 11 is not limited to five, but may be any other suitable number.
- Each of the vaporizing tube panels 16 comprises: a plurality of (in this embodiment, ninety) vaporizing tubes (heat transfer tubes) 21 arranged on a vertical plane and side-by-side to have mutually parallel postures; an inlet-side header (inter-vaporizing tube distribution pipe) 22; a heat-transfer suppressing section 23; and an outlet-side header 24.
- the number of the vaporizing tubes 21 to be comprised in one of the vaporizing tube panels 16 is not limited to ninety, but may be any other suitable number.
- Each of the vaporizing tubes 21 is a tube made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, and formed to extend in an up-down direction.
- the inlet-side header 22 is designed to distribute LNG from the inlet-side manifold 17 to the respective vaporizing tubes 21.
- the inlet-side header 22 is a pipe extending in a horizontal direction along the vertical plane on which the vaporizing tubes 21 are arranged side-by-side.
- the inlet-side header 22 is made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, as with the vaporizing tubes 21.
- the inlet-side header 22 is connected to respective lower ends of the vaporizing tubes 21 comprised in one of the vaporizing tube panels 16.
- the inlet-side header 22 is internally provided with a header inner pipe 50.
- the inlet-side header 22 has one end connected to the inlet-side manifold 17 to allow LNG to be supplied from the inlet-side manifold 17 via the header inner pipe 50 disposed thereinside.
- the header inner pipe 50 is a tubular-shaped member extending along the inlet-side header 22, and is disposed inside the inlet-side header 22 in a coaxial relation to the inlet-side header 22 (see FIG. 3 ).
- the header inner pipe 50 has an outer diameter less than an inner diameter of the inlet-side header 22. Therefore, when the header inner pipe 50 is disposed inside the inlet-side header 22, a given space is defined between an outer peripheral surface of the header inner pipe 50 and an inner peripheral surface of the inlet-side header 22.
- the header inner pipe 50 is connected to the inlet-side manifold 17 to allow LNG to be supplied thereinside.
- the header inner pipe 50 has a plurality of holes 51 formed in a pipe wall (peripheral wall) thereof at positions corresponding to respective ones of the vaporizing tubes 21 along an axial direction of the header inner pipe 50. At each of the positions corresponding to the respective ones of the vaporizing tubes 21 along the axial direction, the hole 51 is provided in a number of two or more (in this embodiment, four).
- the two or more holes 51 at the position corresponding to a respective one of the vaporizing tubes 21 along the axial direction are arranged in a circumferential direction of the header inner pipe 50 in such a manner that a center of each of the holes 51 is located in a lower half of the header inner pipe 50.
- the header inner pipe 50 is provided inside the inlet-side header 22 to form a double-pipe structure, and the plurality of holes 51 are provided in the header inner pipe 50 at positions corresponding to the respective vaporizing tubes 21, so that LNG is distributed to the respective vaporizing tubes 21 at an even flow rate.
- the two or more holes 51 are provided in the header inner pipe 50 at the position corresponding to the respective one of the vaporizing tubes 21, so that a flow of LNG flowing into the vaporizing tube 21 becomes uniform. Specifically, when LNG flows out of the two or more holes 51 at the position corresponding to the respective one of the vaporizing tubes 21, and then flows between the inlet-side header 22 and the header inner pipe 50 toward the vaporizing tube 21, it flows upwardly in the circumferential direction of the inlet-side header 22 and then flows into the vaporizing tube 21.
- the heat-transfer suppressing section 23 is provided on each of opposite ends of the inlet-side header 22.
- the heat-transfer suppressing section 23 is designed to suppress a heat transfer amount per unit area, from seawater to the inlet-side header 22.
- the heat-transfer suppressing section 23 is configured to suppress a heat transfer amount per unit area, when heat of seawater supplied from the seawater supply section 30 is transferred to an overall (entire) second region A2 of the inlet-side header 22.
- the second region A2 of the inlet-side header 22 means a region of the inlet-side header 22 which is located outside a region (first region) A1 where the plurality of vaporizing tubes 21 are arranged, in a longitudinal direction (horizontal direction) of the inlet-side header 22 (see FIGS. 3 and 4 ).
- the first region A1 is a region of the inlet-side header 22 where the plurality of vaporizing tubes 21 are arranged in the longitudinal direction of the inlet-side header 22. That is, it is a region of the inlet-side header 22 between opposite endmost ones of the plurality of vaporizing tubes 21 arranged along the inlet-side header 22, in the longitudinal direction.
- the second region A2 is a region located outside the first region A1 in the longitudinal direction.
- the second region A2 is a region of the inlet-side header 22 located inside the chamber, except the first region A1.
- each of the vaporizing tube blocks 11 is disposed to allow an end of the inlet-side header 22 on a side opposite to the inlet-side manifold 17 is located inside the chamber H.
- the second region A2 consists of a second sub-region A2 located on the side of the inlet-side manifold 17 (in FIG. 3 , on a left side) with respect to the first region A1, and a second sub-region A2 located on a side opposite to the inlet-side manifold 17 (in FIG. 3 , on a right side) with respect to the first region A1.
- the second sub-region A1 on the opposite side is a region ranging from an outer edge of one of the plurality of vaporizing tubes 21 disposed at a right end thereof, to a right end of the inlet-side header 22, in FIG. 4 .
- the second sub-region A2 on the side of the inlet-side manifold is a region ranging from an outer edge of one of the plurality of vaporizing tubes 21 disposed at a left end thereof in FIG. 4 , to a partition wall H1 of the chamber H in which the vaporizing tube blocks 11 are disposed (see FIGS. 1 , 3 and 6 ).
- the heat-transfer suppressing section 23 is a heat insulating member covering the second region A2 of the inlet-side header 22.
- the heat insulating member 23 has a heat conductivity less than that of the inlet-side header 22 (specifically, the pipe wall of the inlet-side header 22).
- the heat insulating member 23 is formed by a tape made of foamed plastic, such as urethane foam, and wound around the inlet-side header 22 to cover a surface of the second region A2. Specifically, the tape has given stretchability. The tape is overlappingly wound around the entire second region A2 of the inlet-side header 22 until a thickness thereof from the surface (outer peripheral surface) of the second region A2 of the inlet-side header 22 becomes 1.5 mm, for example.
- the thickness of the heat insulating member 23 is appropriately set, based on a temperature difference between seawater flowing down toward the first region A1 of the inlet-side header 22 and seawater flowing down toward the second region A2 of the inlet-side header 22, the heat conductivity of the heat insulating member 23 and so on.
- the heat insulating member 23 is provided on only the second region A2, but it is not provided on the first region A1. That is, the first region A1 of the inlet-side header 22 is in an externally exposed state, and the second region A2 is in a state in which it is entirely covered by the heat insulating member 23.
- the heat insulating member 23 is provided on the second region A2 of the inlet-side header 22, so that a heat transfer rate from seawater (specifically, seawater supplied from the seawater supply section 30) to the second region A2 of the inlet-side header 22 is suppressed as compared with a heat transfer rate from the seawater to the first region A1 of the inlet-side header 22.
- the heat insulating member 23 has given stretchability because it is formed by the tape having stretchability.
- the heat insulating member 23 itself expands or shrinks according to the thermal expansion/shrinkage. This makes it possible to effectively prevent damage, such as breakage of the heat insulating member 23 due to thermal expansion/shrinkage of the inlet-side header 22 (particularly, thermal expansion/shrinkage of the inlet-side header 22 in a radial direction thereof).
- the outlet-side header 24 is designed to collect vaporized LNG from the vaporizing tubes 21 and send it to the outlet-side manifold 19.
- the outlet-side header 24 is a pipe extending parallel to the inlet-side header 22.
- the outlet-side header 24 is connected to the vaporizing tubes 21 comprised in one of the vaporizing tube panels 16, and connected to the outlet-side manifold 19.
- the plurality of vaporizing tube panels 16 each configured in the above manner are arranged in a direction (in FIG. 2 , a right-left direction) orthogonal to a panel plane (the vertical plane on which the vaporizing tubes 21 are arranged) to have mutually parallel postures.
- the inlet-side manifold 17 is designed to distribute LNG from the distributing pipe 12, to the respective vaporizing tube panels 16.
- the inlet-side manifold 17 is a pipe extending in a direction intersecting with the inlet-side header 22 (in this embodiment, a direction approximately orthogonal to the inlet-side header 22: a direction perpendicular to a drawing sheet in FIG. 3 ).
- the inlet-side manifold 17 is connected to the respective inlet-side headers 22 comprised in one of the vaporizing tube blocks 11, and is connected to the distributing pipe 12.
- the outlet-side manifold 19 is designed to collect vaporized LNG (i.e., NG) from the vaporizing tube panels 16 and send it to the collecting pipe 14.
- the outlet-side manifold 19 is a pipe extending in a direction intersecting with the outlet-side header 24 (in this embodiment, a direction approximately orthogonal to the outlet-side header 24: a direction perpendicular to a drawing sheet in FIG. 3 ).
- the outlet-side manifold 19 is connected to the respective outlet-side headers 24 comprised in one of the vaporizing tube blocks 11, and is connected to the collecting pipe 14.
- the distributing pipe 12 is a pipe extending approximately parallel to the inlet-side manifold 17.
- the distributing pipe 12 is connected to the respective inlet-side manifolds 17.
- the distributing pipe 12 has an inlet-side connection portion 12a to which a pipe P1 is connected to supply LNG to the vaporizer 10 from the outside.
- the collection pipe 14 is a pipe extending approximately parallel to the outlet-side manifold 19.
- the collection pipe 14 is connected to the respective outlet-side manifolds 19.
- the collecting pipe 14 has an outlet-side connection portion 14a to which a pipe P2 is connected to send NG to the outside, such as a destination for consumption.
- the seawater supply section 30 comprises a trough 31, a seawater header 32 and a seawater manifold 33 (see FIGs. 5A and 5B ).
- the trough 31 is disposed adjacent to an upper end of each of the vaporizing tube panels 16.
- the trough 31 is configured to supplying seawater to the upper end of each of the vaporizing tube panels 16 to allow the seawater to flow down along the surface of the vaporizing tube panel 16 (specifically, the vaporizing tubes 21 constituting the corresponding vaporizing tube panel 16).
- the seawater header 32 is configured to supply seawater to each of a plurality of the troughs 31.
- the seawater manifold 33 is configured to distribute seawater to a plurality of the seawater headers 32.
- the vaporizing tube blocks 11 of the vaporizer 10 configured as above are disposed inside the chamber H surrounded by a wall such as a concrete wall, as illustrated in FIG. 6 .
- each of the vaporizing tube blocks 11 is disposed inside the chamber H in such a manner that the inlet-side manifold 17 and the outlet-side manifold 19 of the vaporizing tube block 11 are located outside the chamber H.
- the chamber H has a partition H1 separating between an inside and outside of the chamber at a position between the set of vaporizing tubes 21 and the inlet-side manifold 17 in the longitudinal direction of the inlet-side header 22.
- the inlet-side header 22 penetrates through the partition wall H1 at a position between an end thereof (on the side of the inlet-side manifold 17) and one of the vaporizing tubes 21 located on the side of the end of the inlet-side header 22, and the outlet-side header 24 penetrates through the partition wall H1 at a position between an end thereof (on the side of the outlet-side manifold 19) and one of the vaporizing tubes 21 located on the side of the end of the outlet-side header 24.
- a heat insulating member is provided to entirely cover a surface of each of the pipes 12, 14, 17, 19 disposed outside the chamber H.
- the vaporizer 10 configured as above is operable to vaporize LNG in the following manner.
- Seawater is supplied from the troughs 31 to respective surfaces of the vaporizing tube panels 16.
- LNG is supplied from a supply pump or the like to the distributing pipe 12 via the pipe P1 connected to the inlet-side connection portion 12a.
- the distributing pipe 12 distributes LNG supplied from the supply pump or the like, to each of the inlet-side manifolds 17 connected to the distributing pipe 12.
- Each of the inlet-side manifolds 17 distributes LNG from the distributing pipe 12, to the respective inlet-side headers 22 connected to the inlet-side manifold 17.
- Each of the inlet-side headers 22 distributes the supplied LNG to the respective vaporizing tubes 21 connected to the inlet-side header 22.
- the LNG supplied from the inlet-side header 22 flows inside of each of the vaporizing tubes 21 in a direction from the lower end to upper end of the vaporizing tube 21.
- the LNG flowing through the vaporizing tube 21 undergoes heat exchange with seawater flowing down along a surface of the vaporizing tube 21, through the tube wall of the vaporizing tube 21. Based on this heat exchange, the LNG is vaporized into NG.
- the seawater supply section 30 supplies seawater to not only a primary region where the vaporizing tubes 21 of the vaporizing tube panel 16 are provided, but also a region outside the primary region in a width direction (an arrangement direction of the vaporizing tubes 21 in the vaporizing tube panels 16). This is intended to allow each of the vaporizing tubes 21 located at opposite endmost positions in the width direction to sufficiently contact seawater in the entire circumference of the vaporizing tubes 21.
- seawater flows down along the vaporizing tube panel 16 toward the first region A1 of the inlet-side header 22, and reaches the inlet-side header 22, it is cooled to a sufficiently low temperature by heat exchange with LNG in the vaporizing tubes 21.
- seawater flowing down outside the vaporizing tubes 21 i.e., flowing down toward the second region A2 of the inlet-side header 22
- the pipe wall in the second region A2 of the inlet-side header 22 has a temperature greater than that of the pipe wall in the first region A1 of the inlet-side header 22 subjected to the heat exchange with water.
- LNG supplied to the vaporizing tube 21 adjacent to the second region A2 (vaporizing tubes 21 at an endmost position in the width direction of the vaporizing tube panel) (specifically, LNG flowing upwardly along the circumferential direction of the inlet-side header 22 when it flowing out of the holes 51 of the header inner pipe 50 and then flowing between the header inner pipe 50 and the inlet-side header 22 toward the vaporizing tube 21) has a temperature greater than that of LNG supplied to he vaporizing tube 21 at a centermost position of the first region A1.
- the heat insulating member 23 is provided on the second region A2 of the inlet-side header 22, so that a heat transfer amount per unit area, from the relatively high-temperature seawater to the pipe wall in the second region A2, is suppressed. This prevents the occurrence of a temperature difference between LNG supplied to the vaporizing tube 21 adjacent to the second region A2 of the inlet-side header 22, and LNG supplied to the vaporizing tube 21 at a centermost position of the first region A1 of the inlet-side header 22.
- Vaporized LNG, i.e., NG, from the vaporizing tubes 21, is collected by the outlet-side header 24, and sent to the outlet-side manifold 19.
- the NG sent to the outlet-side manifold 19 is sent to a destination for consumption or the like, via the collecting pipe 14, and the pipe P2 connected to the outlet-side connection portion 14a.
- the heat insulating member (heat-transfer suppressing section) 23 functions to suppress a heat transfer amount per unit area, from seawater to the overall second region A2 of the inlet-side header 22 (a region of the inlet-side header 22 inside the chamber H housing the vaporizing tube blocks 11, except the first region A1).
- the heat insulating member (heat-transfer suppressing section) 23 functions to suppress a heat transfer amount per unit area, from seawater to the overall second region A2 of the inlet-side header 22 (a region of the inlet-side header 22 inside the chamber H housing the vaporizing tube blocks 11, except the first region A1).
- the overall (entire) second region A2 of the inlet-side header 22 is surrounded by the heat insulating member 23. This makes it possible to suppress a heat transfer amount per unit area from seawater to the second region A2 of the inlet-side header 22, as compared to a heat transfer amount per unit area from seawater to the first region A1 of the inlet-side header 22, in an easy and reliable manner.
- the heat insulating member 23 has given stretchability, so that it becomes possible to prevent damage of the heat insulating member 23 due to thermal expansion/shrinkage of the inlet-side header 22.
- the inlet-side header 22 thermally expands or shrinks due to a temperature difference between during operation of the vaporizer 10 and during stopping of the vaporizer 10.
- the heat insulating member 23 surrounding the inlet-side header 22 has given stretchability, so that it can stretch or contract according to thermal expansion/shrinkage of the inlet-side header 22. This makes it possible to effectively prevent damage of the heat insulating member 23 due to thermal expansion/shrinkage (particularly, thermal expansion/shrinkage in the radial direction) of the inlet-side header 22.
- An inlet-side header of this vaporizer is made of aluminum and formed to have an outer diameter of 165.2 mm.
- the inlet-side header has a heat transfer rate of 5000 W/mK.
- the heat insulating member has a heat conductivity of 1W/mK.
- a temperature of LNG flowing the second region of the above inlet-side header was measured while supplying LNG having a temperature of - 145°C, to the inlet-side header, under the following three conditions: without any heat insulating member; with a heat insulating member having a thickness of 0.5 mm; and with a heat insulating member having a thickness of 1.5 mm.
- a result of the measurement is illustrated in FIG. 7 .
- the graph in FIG. 7 shows that a temperature rise of LNG flowing through the inlet-side header due to seawater can be suppressed by providing a heat insulating member on the second region of the inlet-side header even if the heat insulating member has a relatively small thickness, as compared to the case without any heat insulating member.
- cryogenic liquid vaporizer of the present invention is not limited to the above embodiment, but it is to be understood that various changes and modifications may be made therein without departing from the scope thereof as set forth in appended claims
- a specific configuration of the heat insulating member 23 is not particularly limited.
- the heat insulating member 23 in the above embodiment is formed by overlappingly winding (wrapping) a tape made of foamed plastic such as urethane foam, around the second region A2 of the inlet-side header 22, it is not limited thereto. That is, as illustrated in FIG. 8 , the heat insulating member may be tubular and bottomed tubular-shaped members 23A, 23B each made of a material having relatively small heat conductivity (e.g., resin such silicon resin or polyvinyl chloride resin; foamed rein; or resin incorporating glass fiber or rubber).
- Each of the tubular-shaped heat insulating member 23A and the bottomed tubular-shaped heat insulating member 23B has an inner peripheral surface 123 with a diameter (inner diameter) corresponding to a diameter (outer diameter) of an outer peripheral surface of the second region A2 of the inlet-side header 22, or with an inner diameter greater than the outer diameter.
- the tubular-shaped heat insulating member 23A is fit on the second sub-region A2 of the inlet-side header 22 on the side of the inlet-side manifold 17.
- the bottomed tubular-shaped heat insulating member 23B is fit on the second sub-region A2 of the inlet-side header 22 on a side opposite to the inlet-side manifold 17. In this manner, the overall second region A2 is surrounded by the insulating members 23A, 23B.
- the heat insulating member may be formed by foamed plastic, such as urethane foam, sprayed onto the surface of the second region A2 of the inlet-side header 22 to have a given thickness.
- the heat-transfer suppressing section is not limited to the configuration surrounding the second region A2 of the inlet-side header 22.
- the heat-transfer suppressing section may be a cover member 60 (see FIG. 9 ) disposed on an upper side of the second region A2 of the inlet-side header 22, and formed in a shape capable of covering over the second region A2 of the inlet-side header 22, in top plan view.
- This cover member 60 has a width (in a horizontal direction) greater than the outer diameter of the inlet-side header 22 so as to cover over the second region A2 of the inlet-side header 22, in top plan view.
- cover member 60 is disposed on the upper side of the second region A2 of the inlet-side header 22, in spaced-apart relation to (or in contact with) the second region A2.
- the above configuration can prevent seawater flowing down outside the vaporizing tube at the endmost position in the longitudinal direction of the inlet-side header (horizontal direction) and undergoing almost no heat exchange with LNG flowing through the vaporizing tube, from hitting against the second region of the inlet-side header.
- the pipe wall of the second region A2 of the inlet-side header may be made of a material having a heat conductivity less than that of the pipe wall of the first region A1 of the inlet-side header.
- the pipe wall of the first region A1 may be made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, as with the first embodiment, and the pipe wall of the second region A2 may be made of iron or SUS.
- only the pipe wall in the second region A2 of the inlet-side header 22 may be formed in a layered structure in a thickness direction of the pipe wall.
- This configuration can suppress heat conductivity in a direction from s surface (outer peripheral surface) of the second region A2 of the inlet-side header to an inside of the second region A2 (inner peripheral surface of the inlet-side header), so that a heat conductivity (equivalent heat conductivity) of the pipe wall of the second region A2 of the inlet-side header 22 becomes less than that of the pipe wall of the first region A1 of the inlet-side header 22.
- a heat conductivity equivalent heat conductivity
- the pipe wall of the second region A2 of the inlet-side header 22 is composed of a plurality of layers (in the embodiments illustrated in FIG. 10 , two layers), and a heat-transfer suppressing layer 62 filled with air or a heat insulating material is formed between the layers.
- a heat conductivity (equivalent heat conductivity) in the pipe wall of the second region A2 of the inlet-side header 22 becomes less than that in the pipe wall of the first region A1 of the inlet-side header 22.
- the number of layers constituting the pipe wall may be three or more.
- the header inner pipe 50 is provided inside the inlet-side header 22.
- the vaporizer is not limited to this configuration. That is, the vaporizer may be configured to allow LNG to be directly supplied from the inlet-side manifold 17 to the inlet-side header 22, without providing the header inner pipe 50.
- cryogenic liquid vaporizer of the present invention is useful for vaporizing a cryogenic liquid, such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN 2 ), by means of heat exchange with a heat medium such as seawater, and suited to suppress bending deformation due to a difference in temperature of the inter-vaporizing tube distribution pipe in a longitudinal direction thereof.
- a cryogenic liquid such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN 2 .
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Description
- The present invention relates to a vaporizer for vaporizing a cryogenic liquid, such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN2), by means of heat exchange with a heat medium such as seawater.
- Heretofore, there has been known a vaporizer (ORV) for vaporizing a liquefied natural gas (LNG) by means of heat exchange with seawater (heat-exchanging liquid), as disclosed in the following
Patent Document 1. - As illustrated in
FIG. 11 , this vaporizer comprises a vaporizingtube panel 102 extending along a specific vertical plane, and aseawater supply section 104 for supplying seawater to the vaporizingtube panel 102. - The vaporizing
tube panel 102 comprises a plurality of vaporizing tubes (heat transfer tubes) 106, and an inter-vaporizing tube distribution pipe (inlet-side header) 108. Theseawater supply section 104 is designed to supply seawater from an upper end of the vaporizingtube panel 102 to allow the seawater to flow down along a surface of the vaporizingtube panel 102. - Each of the vaporizing
tubes 106 is disposed to extend in a vertical direction to allow a liquefied natural gas (cryogenic liquid) to flow therethrough so as to cause a heat exchange with an external medium, thereby vaporizing the liquefied natural gas. The plurality of vaporizingtubes 106 comprised in the vaporizingtube panel 102 are arranged on the specific vertical plane and side-by-side in a horizontal direction to have mutually parallel postures. The inter-vaporizingtube distribution pipe 108 is designed to distribute liquefied natural gas to the respective vaporizingtubes 106 comprised in the vaporizingtube panel 102. The inter-vaporizingtube distribution pipe 108 is disposed to extend in the horizontal direction and connected to respective lower ends of the vaporizingtubes 106 comprised in the vaporizingtube panel 102. - In this type of
vaporizer 100, the inter-vaporizingtube distribution pipe 108 distributes liquefied natural gas to the respective vaporizingtubes 106, and the distributed liquefied natural gas flows through each of the vaporizingtubes 106 upwardly. Concurrently, seawater supplied from theseawater supply section 104 flows down along and outside the vaporizingtubes 106. In this process, in each of the vaporizingtubes 106, heat exchange is performed between the liquefied natural gas and the seawater, through a tube wall of the vaporizingtube 106 separating an inside and an outside thereof. This allows the liquefied natural gas to be vaporized into natural gas (NG). - There has also been a vaporizer described in the following Patent Document 2. As illustrated in
FIG. 12 , in this vaporizer, awater protection cover 110 is disposed to cover an upper side of a first region a1 of the inter-vaporizingtube distribution pipe 108. Thewater protection cover 110 is designed to prevent seawater from directly hitting against the first region a1 of the inter-vaporizingtube distribution pipe 108. This makes it possible to suppress a fluctuation in heat amount of liquefied natural gas (vaporized liquefied natural gas) when the vaporizer is operated at a low load under a condition that a temperature of seawater is relatively high. - In the vaporizer disclosed in the
Patent Document 1, when a cryogenic liquid (liquefied natural gas) is vaporized, a difference in temperature occurs between an end (region a2 inFIG. 11 ) and a central portion (region a2 inFIG. 11 ) of the inter-vaporizingtube distribution pipe 108 in a longitudinal direction of thedistribution pipe 108. If such a temperature difference occurs, the inter-vaporizingtube distribution pipe 108 is likely to undergo bending deformation, due to a difference in amount of thermal expansion/shrinkage in each of the vaporizingtubes 106 caused by the temperature difference. This results in the occurrence of warpage in the inter-vaporizingtube distribution pipe 108, and the occurrence of stress in a joining area between the inter-vaporizingtube distribution pipe 108 and each of the vaporizingtubes 106. - Specifically, a temperature in a region located longitudinally outside a region a1 of the inter-vaporizing
tube distribution pipe 108 where the plurality of vaporizingtubes 106 are arranged becomes greater than a temperature in the region a1. That is, in the inter-vaporizingtube distribution pipe 108, a temperature of a longitudinal end a2 becomes greater than a temperature of the region a1. This is based on the following reason. - When a heat-exchanging liquid (seawater) flowing down within the first region a1 along the vaporizing
tube panel 102 a1 reaches the inter-vaporizingtube distribution pipe 108, it is cooled to a sufficiently low temperature by heat exchange with the cryogenic liquid in the vaporizingtubes 106. On the other hand, a heat-exchanging liquid flowing down outside the vaporizingtube panel 102 in the longitudinal direction undergoes almost no heat exchange with the cryogenic liquid in the vaporizingtubes 106. Thus, when the heat-exchanging liquid reaches the inter-vaporizingtube distribution pipe 108, it has a temperature greater than that of heat-exchanging liquid flowing down within the first region a1. - When a temperature difference occurs between the first region a1 and the second region a2 of the inter-vaporizing
tube distribution pipe 108 as described above, a difference occurs between a temperature of cryogenic liquid distributed from the inter-vaporizingtube distribution pipe 108 to one of the vaporizingtubes 106 located at an endmost position of the first region a1 in the longitudinal direction, and a temperature of cryogenic liquid distributed from the inter-vaporizingtube distribution pipe 108 to one of the remaining vaporizingtubes 106 located at a centermost position of the first region a1 in the longitudinal direction. As a result, a difference in amount of thermal expansion/shrinkage occurs between the vaporizingtube 106 at the endmost position and the vaporizingtube 106 at the centermost position, so that the inter-vaporizingtube distribution pipe 108 undergoes bending deformation. - In the vaporizer described in the Parent Document 2, the
water protection cover 110 can prevent the heat-exchanging liquid from directly hitting against the first region a1 of the inter-vaporizingtube distribution pipe 108. However, in the second region a2 of the inter-vaporizingtube distribution pipe 108, thewater protection cover 110 covers only a region adjacent to the vaporizingtube 106 at the endmost position, in the horizontal direction. Thus, in this vaporizer, a (relatively high-temperature) heat-exchanging liquid subjected to no heat exchange with the cryogenic liquid also hits against the second region a2 of the inter-vaporizingtube distribution pipe 108. Therefore, in this vaporizer, a temperature difference occurs between the first region a1 and the second region a2 of the inter-vaporizingtube distribution pipe 108. As a result, in the vaporizer described in the Patent Document 2, there is a concern that the inter-vaporizingtube distribution pipe 108 undergoes bending deformation, as with the vaporizer in thePatent Document 1. - Patent Document 3 discloses a cryogenic liquid vaporizer having the features defined in the preambles of
claims 1 and 6. - Other conventional vaporizers are known from Patent Documents 4 to 8. Among others, Patent Documents 4 to 7 suggest suppressing heat transfer from the heat-exchanging liquid to a region of the inter-vaporizing tube distribution tube where the vaporizing tubes are arranged.
-
- Patent Document 1:
JP S57-057998A - Patent Document 2:
JP H08-183970A - Patent Document 3:
JP H08-029075 A - Patent Document 4:
JP H03-386990 A - Patent Document 5:
JP H03-317996 A - Patent Document 6:
JP H06-26783 A - Patent Document 7:
JP 2007-16968 A - Patent Document 8:
WO 96/02803 A1 - It is an object of the present invention to provide a cryogenic liquid vaporizer which allows an inter-vaporizing tube distribution pipe to become less likely to undergo bending deformation due to a difference in temperature of the inter-vaporizing tube distribution pipe in a longitudinal direction thereof.
- According to one aspect of the present invention, there is provided a cryogenic liquid vaporizer for vaporizing a cryogenic liquid, which comprises the features defined in
claim 1. - In the cryogenic liquid vaporizer according to the above aspect, even in a situation where the heat-exchanging liquid flowing down toward the second region of the inter-vaporizing tube distribution pipe has a temperature greater than that of the heat-exchanging liquid flowing down toward the first region of the inter-vaporizing tube distribution pipe, the heat-transfer suppressing section functions to suppress a heat transfer amount per unit area, from the heat-exchanging liquid to the second region. Thus, it becomes possible to prevent a temperature in the second region of the inter-vaporizing tube distribution pipe from becoming greater than that in the first region of the inter-vaporizing tube distribution pipe. This makes it possible to suppress a temperature difference between the cryogenic liquid distributed from the inter-vaporizing tube distribution pipe to the vaporizing tube at an endmost position of the vaporizing tube panel in the horizontal direction thereof, and LNG distributed from the inter-vaporizing tube distribution pipe to the vaporizing tube at a centermost position of the first region, so that it becomes possible to prevent bending deformation of the inter-vaporizing tube distribution pipe due to amounts of thermal expansion/shrinkage in the vaporizing tubes.
- In the cryogenic liquid vaporizer according to the above aspect, the heat-transfer suppressing section may be a heat insulating member surrounding the second region of the inter-vaporizing tube distribution pipe, wherein the heat insulating member has a heat conductivity less than a heat conductivity of the inter-vaporizing tube distribution pipe.
- This configuration makes it possible to suppress a heat transfer amount per unit area from the heat-exchanging liquid to the second region of the inter-vaporizing tube distribution pipe, as compared to a heat transfer amount per unit area from the heat-exchanging liquid to the first region of the inter-vaporizing tube distribution pipe, in an easy and reliable manner.
- In this case, it is preferable that the heat insulating member has given stretchability.
- This configuration makes it possible to prevent damage of the heat insulating member due to thermal expansion/shrinkage of the inter-vaporizing tube distribution pipe. Specifically, the heat insulating member surrounding the inter-vaporizing tube distribution pipe has given stretchability. Thus, when the inter-vaporizing tube distribution pipe thermally expands or shrinks due to a temperature difference between when the cryogenic liquid is flowing (i.e., during operation of the vaporizer) and when the cryogenic liquid is not flowing (i.e., during stopping of the vaporizer), the heat insulating member can stretch or contract according to thermal expansion/shrinkage of the inter-vaporizing tube distribution pipe. This makes it possible to effectively prevent damage of the heat insulating member due to thermal expansion/shrinkage (particularly, thermal expansion/shrinkage in a radial direction) of the inter-vaporizing tube distribution pipe.
- The heat-transfer suppressing section may be a cover member which is disposed on an upper side of the second region of the inter-vaporizing tube distribution pipe, and formed in a shape capable of covering over the second region of the inter-vaporizing tube distribution pipe, in top plan view.
- This configuration can prevent the heat-exchanging liquid flowing down outside the vaporizing tube at the endmost position in a longitudinal direction of the inter-vaporizing tube distribution pipe (horizontal direction) and undergoing almost no heat exchange with the cryogenic liquid flowing through the vaporizing tube, from hitting against the second region of the inter-vaporizing tube distribution pipe. This makes it possible to prevent the occurrence of a temperature difference between the first region and the second region in the inter-vaporizing tube distribution pipe.
- When a portion of the inter-vaporizing tube distribution pipe between one end thereof and one of the vaporizing tubes located on the side of the one end is disposed to penetrate through a partition wall, the second region is a region between the partition wall and the vaporizing tube located on the side of the one end.
- According to another aspect of the present invention, there is provided a cryogenic liquid vaporizer for vaporizing a cryogenic liquid, which comprises the features defined in claim 6.
- In this configuration, the heat conductivity of the pipe wall in the second region of the inter-vaporizing tube distribution pipe is less than that of the pipe wall in the first region of the inter-vaporizing tube distribution pipe, so that, even when a heat-exchanging liquid having a temperature greater than that of the first region of the inter-vaporizing tube distribution pipe hits against the second region of the inter-vaporizing tube distribution pipe, it becomes possible to prevent the occurrence of a temperature difference between the cryogenic liquid flowing through the first region of the inter-vaporizing tube distribution pipe, and the cryogenic liquid flowing through the second region of the inter-vaporizing tube distribution pipe. This makes it possible to prevent bending deformation of the inter-vaporizing tube distribution pipe due to the above temperature difference.
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-
FIG. 1 is a schematic perspective view of a cryogenic liquid vaporizer according to one embodiment of the present invention. -
FIG. 2 is a schematic diagram (front view) illustrating a state of a pipe arrangement of the vaporizer. -
FIG. 3 is a schematic diagram (side view) illustrating the state of the pipe arrangement of the vaporizer. -
FIG. 4 is a fragmentary enlarged view for explaining a heat-transfer suppressing section of the vaporizer. -
FIG. 5A is a side view for explaining a seawater supply section of the vaporizer, andFIG. 5B is a front view for explaining the seawater supply section of the vaporizer. -
FIG. 6 is a partially-broken perspective view illustrating an installed state of the vaporizer. -
FIG. 7 is a graph presenting a difference in temperature of liquefied natural gas flowing through an inlet-side header, depending on a thickness of a heat insulating member. -
FIG. 8 is a vertical sectional view for explaining a heat insulating member (heat-transfer suppressing section) in another embodiment. -
FIG. 9 is an enlarged cross-sectional view for explaining a cover member in a cryogenic liquid vaporizer according to another embodiment. -
FIG. 10 is an enlarged cross-sectional view of a second region of an inter-vaporizing tube distribution pipe in a cryogenic liquid vaporizer according to another embodiment. -
FIG. 11 is a fragmentary enlarged perspective view for explaining a conventional vaporizer. -
FIG. 12 is a fragmentary enlarged perspective view for explaining a conventional vaporizer. - With reference to the accompanying drawings, the present invention will now be described based on one embodiment of the present invention.
- A cryogenic liquid vaporizer (hereinafter also referred to simply as "vaporizer") according to this embodiment is a so-called open rack vaporize (ORV) for subjecting a supplied cryogenic liquid to heat exchange with an external heat-exchanging liquid to thereby vaporize the cryogenic liquid. The vaporizer according to this embodiment is designed to vaporize a liquefied natural gas (LNG). The heat-exchanging liquid for use in this embodiment is seawater.
- Specifically, as illustrated in
FIGS. 1 to 5 , the vaporizer comprises a plurality of (in this embodiment, two) vaporizing tube blocks 11, a distributingpipe 12, a collectingpipe 14, and a seawater supply section (liquid supply section) 30. The distributingpipe 12 is designed to distribute LNG to the respective vaporizing tube blocks 11. The collectingpipe 14 is designed to collect vaporized LNG (natural gas (NG)) from the vaporizing tube blocks 11. Theseawater supply section 30 is designed to supply seawater to an upper portion of each of a plurality of aftermentionedvaporizing tube panels 16 to allow the seawater to flow down along a surface of the vaporizingtube panel 16. The number of the vaporizing tube blocks 11 to be provided in thevaporizer 10 is not limited to two or more, but may be one. - Each of the components will be described below in detail.
- Each of the vaporizing tube blocks 11 comprises a plurality of (in this embodiment, five) vaporizing
tube panels 16, an inlet-side manifold 17, and an outlet-side manifold 19. The number of the vaporizingtube panels 16 to be comprised in one of the vaporizing tube blocks 11 is not limited to five, but may be any other suitable number. - Each of the vaporizing
tube panels 16 comprises: a plurality of (in this embodiment, ninety) vaporizing tubes (heat transfer tubes) 21 arranged on a vertical plane and side-by-side to have mutually parallel postures; an inlet-side header (inter-vaporizing tube distribution pipe) 22; a heat-transfer suppressing section 23; and an outlet-side header 24. The number of the vaporizingtubes 21 to be comprised in one of the vaporizingtube panels 16 is not limited to ninety, but may be any other suitable number. - Each of the vaporizing
tubes 21 is a tube made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, and formed to extend in an up-down direction. - The inlet-
side header 22 is designed to distribute LNG from the inlet-side manifold 17 to therespective vaporizing tubes 21. Specifically, the inlet-side header 22 is a pipe extending in a horizontal direction along the vertical plane on which the vaporizingtubes 21 are arranged side-by-side. The inlet-side header 22 is made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, as with the vaporizingtubes 21. The inlet-side header 22 is connected to respective lower ends of the vaporizingtubes 21 comprised in one of the vaporizingtube panels 16. The inlet-side header 22 is internally provided with a headerinner pipe 50. The inlet-side header 22 has one end connected to the inlet-side manifold 17 to allow LNG to be supplied from the inlet-side manifold 17 via the headerinner pipe 50 disposed thereinside. - The header
inner pipe 50 is a tubular-shaped member extending along the inlet-side header 22, and is disposed inside the inlet-side header 22 in a coaxial relation to the inlet-side header 22 (seeFIG. 3 ). The headerinner pipe 50 has an outer diameter less than an inner diameter of the inlet-side header 22. Therefore, when the headerinner pipe 50 is disposed inside the inlet-side header 22, a given space is defined between an outer peripheral surface of the headerinner pipe 50 and an inner peripheral surface of the inlet-side header 22. The headerinner pipe 50 is connected to the inlet-side manifold 17 to allow LNG to be supplied thereinside. The headerinner pipe 50 has a plurality ofholes 51 formed in a pipe wall (peripheral wall) thereof at positions corresponding to respective ones of the vaporizingtubes 21 along an axial direction of the headerinner pipe 50. At each of the positions corresponding to the respective ones of the vaporizingtubes 21 along the axial direction, thehole 51 is provided in a number of two or more (in this embodiment, four). Specifically, the two ormore holes 51 at the position corresponding to a respective one of the vaporizingtubes 21 along the axial direction (in this embodiment, at a position on a lower side of the vaporizing tube 21) are arranged in a circumferential direction of the headerinner pipe 50 in such a manner that a center of each of theholes 51 is located in a lower half of the headerinner pipe 50. - As above, the header
inner pipe 50 is provided inside the inlet-side header 22 to form a double-pipe structure, and the plurality ofholes 51 are provided in the headerinner pipe 50 at positions corresponding to therespective vaporizing tubes 21, so that LNG is distributed to therespective vaporizing tubes 21 at an even flow rate. - In addition, the two or
more holes 51 are provided in the headerinner pipe 50 at the position corresponding to the respective one of the vaporizingtubes 21, so that a flow of LNG flowing into the vaporizingtube 21 becomes uniform. Specifically, when LNG flows out of the two ormore holes 51 at the position corresponding to the respective one of the vaporizingtubes 21, and then flows between the inlet-side header 22 and the headerinner pipe 50 toward the vaporizingtube 21, it flows upwardly in the circumferential direction of the inlet-side header 22 and then flows into the vaporizingtube 21. Thus, as compared to the case where LNG flows out of holes provided in an upper portion of the header inner pipe 50 (e.g., at positions opposed to the lower end of the vaporizing tube 21) and immediately flows into the vaporizingtube 21, a flow of LNG becomes uniform. - The heat-
transfer suppressing section 23 is provided on each of opposite ends of the inlet-side header 22. The heat-transfer suppressing section 23 is designed to suppress a heat transfer amount per unit area, from seawater to the inlet-side header 22. Specifically, the heat-transfer suppressing section 23 is configured to suppress a heat transfer amount per unit area, when heat of seawater supplied from theseawater supply section 30 is transferred to an overall (entire) second region A2 of the inlet-side header 22. - As used here, the second region A2 of the inlet-
side header 22 means a region of the inlet-side header 22 which is located outside a region (first region) A1 where the plurality of vaporizingtubes 21 are arranged, in a longitudinal direction (horizontal direction) of the inlet-side header 22 (seeFIGS. 3 and4 ). - The first region A1 is a region of the inlet-
side header 22 where the plurality of vaporizingtubes 21 are arranged in the longitudinal direction of the inlet-side header 22. That is, it is a region of the inlet-side header 22 between opposite endmost ones of the plurality of vaporizingtubes 21 arranged along the inlet-side header 22, in the longitudinal direction. On the other hand, the second region A2 is a region located outside the first region A1 in the longitudinal direction. For example, when the vaporizing tube blocks 11 are disposed within a chamber H (seeFIG. 6 ), the second region A2 is a region of the inlet-side header 22 located inside the chamber, except the first region A1. In this case, each of the vaporizing tube blocks 11 is disposed to allow an end of the inlet-side header 22 on a side opposite to the inlet-side manifold 17 is located inside the chamber H. - More specifically, the second region A2 consists of a second sub-region A2 located on the side of the inlet-side manifold 17 (in
FIG. 3 , on a left side) with respect to the first region A1, and a second sub-region A2 located on a side opposite to the inlet-side manifold 17 (inFIG. 3 , on a right side) with respect to the first region A1. The second sub-region A1 on the opposite side is a region ranging from an outer edge of one of the plurality of vaporizingtubes 21 disposed at a right end thereof, to a right end of the inlet-side header 22, inFIG. 4 . On the other hand, the second sub-region A2 on the side of the inlet-side manifold is a region ranging from an outer edge of one of the plurality of vaporizingtubes 21 disposed at a left end thereof inFIG. 4 , to a partition wall H1 of the chamber H in which the vaporizing tube blocks 11 are disposed (seeFIGS. 1 ,3 and6 ). - The heat-
transfer suppressing section 23 is a heat insulating member covering the second region A2 of the inlet-side header 22. Theheat insulating member 23 has a heat conductivity less than that of the inlet-side header 22 (specifically, the pipe wall of the inlet-side header 22). Theheat insulating member 23 is formed by a tape made of foamed plastic, such as urethane foam, and wound around the inlet-side header 22 to cover a surface of the second region A2. Specifically, the tape has given stretchability. The tape is overlappingly wound around the entire second region A2 of the inlet-side header 22 until a thickness thereof from the surface (outer peripheral surface) of the second region A2 of the inlet-side header 22 becomes 1.5 mm, for example. The thickness of theheat insulating member 23 is appropriately set, based on a temperature difference between seawater flowing down toward the first region A1 of the inlet-side header 22 and seawater flowing down toward the second region A2 of the inlet-side header 22, the heat conductivity of theheat insulating member 23 and so on. - In the inlet-
side header 22, theheat insulating member 23 is provided on only the second region A2, but it is not provided on the first region A1. That is, the first region A1 of the inlet-side header 22 is in an externally exposed state, and the second region A2 is in a state in which it is entirely covered by theheat insulating member 23. - In this way, the
heat insulating member 23 is provided on the second region A2 of the inlet-side header 22, so that a heat transfer rate from seawater (specifically, seawater supplied from the seawater supply section 30) to the second region A2 of the inlet-side header 22 is suppressed as compared with a heat transfer rate from the seawater to the first region A1 of the inlet-side header 22. This allows a temperature of the pipe wall of the second region A2 of the inlet-side header 22 to be kept from becoming greater than a temperature of the pipe wall of the first region A1 of the inlet-side header 22, even if seawater flowing down toward the second region of the inlet-side header 22 has a temperature greater than of seawater flowing down from theseawater supply section 30 toward the first region A1 of the inlet-side header 22. - In addition, the
heat insulating member 23 has given stretchability because it is formed by the tape having stretchability. Thus, even when the inlet-side header 22 thermally expands or shrinks, theheat insulating member 23 itself expands or shrinks according to the thermal expansion/shrinkage. This makes it possible to effectively prevent damage, such as breakage of theheat insulating member 23 due to thermal expansion/shrinkage of the inlet-side header 22 (particularly, thermal expansion/shrinkage of the inlet-side header 22 in a radial direction thereof). - The outlet-
side header 24 is designed to collect vaporized LNG from the vaporizingtubes 21 and send it to the outlet-side manifold 19. The outlet-side header 24 is a pipe extending parallel to the inlet-side header 22. The outlet-side header 24 is connected to the vaporizingtubes 21 comprised in one of the vaporizingtube panels 16, and connected to the outlet-side manifold 19. - The plurality of vaporizing
tube panels 16 each configured in the above manner are arranged in a direction (inFIG. 2 , a right-left direction) orthogonal to a panel plane (the vertical plane on which the vaporizingtubes 21 are arranged) to have mutually parallel postures. - The inlet-
side manifold 17 is designed to distribute LNG from the distributingpipe 12, to the respectivevaporizing tube panels 16. The inlet-side manifold 17 is a pipe extending in a direction intersecting with the inlet-side header 22 (in this embodiment, a direction approximately orthogonal to the inlet-side header 22: a direction perpendicular to a drawing sheet inFIG. 3 ). The inlet-side manifold 17 is connected to the respective inlet-side headers 22 comprised in one of the vaporizing tube blocks 11, and is connected to the distributingpipe 12. - The outlet-
side manifold 19 is designed to collect vaporized LNG (i.e., NG) from the vaporizingtube panels 16 and send it to the collectingpipe 14. The outlet-side manifold 19 is a pipe extending in a direction intersecting with the outlet-side header 24 (in this embodiment, a direction approximately orthogonal to the outlet-side header 24: a direction perpendicular to a drawing sheet inFIG. 3 ). The outlet-side manifold 19 is connected to the respective outlet-side headers 24 comprised in one of the vaporizing tube blocks 11, and is connected to the collectingpipe 14. - The distributing
pipe 12 is a pipe extending approximately parallel to the inlet-side manifold 17. The distributingpipe 12 is connected to the respective inlet-side manifolds 17. The distributingpipe 12 has an inlet-side connection portion 12a to which a pipe P1 is connected to supply LNG to thevaporizer 10 from the outside. - The
collection pipe 14 is a pipe extending approximately parallel to the outlet-side manifold 19. Thecollection pipe 14 is connected to the respective outlet-side manifolds 19. The collectingpipe 14 has an outlet-side connection portion 14a to which a pipe P2 is connected to send NG to the outside, such as a destination for consumption. - The
seawater supply section 30 comprises atrough 31, aseawater header 32 and a seawater manifold 33 (seeFIGs. 5A and 5B ). Thetrough 31 is disposed adjacent to an upper end of each of the vaporizingtube panels 16. Thetrough 31 is configured to supplying seawater to the upper end of each of the vaporizingtube panels 16 to allow the seawater to flow down along the surface of the vaporizing tube panel 16 (specifically, the vaporizingtubes 21 constituting the corresponding vaporizing tube panel 16). Seawater (medium outside of the vaporizing tubes 21) supplied from thetrough 31 to flow down along the surface of the vaporizingtube panel 16, and LNG flowing inside of the vaporizingtubes 21, are heat-exchanged through respective tube walls of the vaporizingtubes 21. Consequently, LNG is vaporized into NG. Theseawater header 32 is configured to supply seawater to each of a plurality of thetroughs 31. Theseawater manifold 33 is configured to distribute seawater to a plurality of theseawater headers 32. - The vaporizing tube blocks 11 of the
vaporizer 10 configured as above are disposed inside the chamber H surrounded by a wall such as a concrete wall, as illustrated inFIG. 6 . Specifically, each of the vaporizing tube blocks 11 is disposed inside the chamber H in such a manner that the inlet-side manifold 17 and the outlet-side manifold 19 of the vaporizingtube block 11 are located outside the chamber H. The chamber H has a partition H1 separating between an inside and outside of the chamber at a position between the set of vaporizingtubes 21 and the inlet-side manifold 17 in the longitudinal direction of the inlet-side header 22. The inlet-side header 22 penetrates through the partition wall H1 at a position between an end thereof (on the side of the inlet-side manifold 17) and one of the vaporizingtubes 21 located on the side of the end of the inlet-side header 22, and the outlet-side header 24 penetrates through the partition wall H1 at a position between an end thereof (on the side of the outlet-side manifold 19) and one of the vaporizingtubes 21 located on the side of the end of the outlet-side header 24. A heat insulating member is provided to entirely cover a surface of each of thepipes - The
vaporizer 10 configured as above is operable to vaporize LNG in the following manner. - Seawater is supplied from the
troughs 31 to respective surfaces of the vaporizingtube panels 16. Concurrently, LNG is supplied from a supply pump or the like to the distributingpipe 12 via the pipe P1 connected to the inlet-side connection portion 12a. The distributingpipe 12 distributes LNG supplied from the supply pump or the like, to each of the inlet-side manifolds 17 connected to the distributingpipe 12. Each of the inlet-side manifolds 17 distributes LNG from the distributingpipe 12, to the respective inlet-side headers 22 connected to the inlet-side manifold 17. Each of the inlet-side headers 22 distributes the supplied LNG to therespective vaporizing tubes 21 connected to the inlet-side header 22. The LNG supplied from the inlet-side header 22 flows inside of each of the vaporizingtubes 21 in a direction from the lower end to upper end of the vaporizingtube 21. In this process, the LNG flowing through the vaporizingtube 21 undergoes heat exchange with seawater flowing down along a surface of the vaporizingtube 21, through the tube wall of the vaporizingtube 21. Based on this heat exchange, the LNG is vaporized into NG. - When the vaporization of LNG is being performed in the
vaporizer 10, theseawater supply section 30 supplies seawater to not only a primary region where the vaporizingtubes 21 of the vaporizingtube panel 16 are provided, but also a region outside the primary region in a width direction (an arrangement direction of the vaporizingtubes 21 in the vaporizing tube panels 16). This is intended to allow each of the vaporizingtubes 21 located at opposite endmost positions in the width direction to sufficiently contact seawater in the entire circumference of the vaporizingtubes 21. Thus, when LNG is vaporized into NG, i.e., during operation of thevaporizer 10, seawater flows down along the vaporizingtube panel 16 toward the first region A1 of the inlet-side header 22, and reaches the inlet-side header 22, it is cooled to a sufficiently low temperature by heat exchange with LNG in the vaporizingtubes 21. On the other hand, seawater flowing down outside the vaporizing tubes 21 (i.e., flowing down toward the second region A2 of the inlet-side header 22) undergoes almost no heat exchange with LNG in the vaporizingtubes 21, so that a temperature of the seawater reaching the inlet-side header 22 is greater than that of water flowing down toward the first region A1. Thus, supposing that the heat insulating member (heat-transfer suppressing section) 23 is not provided on the second region A2 of the inlet-side header 22, the pipe wall in the second region A2 of the inlet-side header 22 has a temperature greater than that of the pipe wall in the first region A1 of the inlet-side header 22 subjected to the heat exchange with water. Therefore, LNG supplied to the vaporizingtube 21 adjacent to the second region A2 (vaporizingtubes 21 at an endmost position in the width direction of the vaporizing tube panel) (specifically, LNG flowing upwardly along the circumferential direction of the inlet-side header 22 when it flowing out of theholes 51 of the headerinner pipe 50 and then flowing between the headerinner pipe 50 and the inlet-side header 22 toward the vaporizing tube 21) has a temperature greater than that of LNG supplied to he vaporizingtube 21 at a centermost position of the first region A1. However, in thevaporizer 10 according to this embodiment, theheat insulating member 23 is provided on the second region A2 of the inlet-side header 22, so that a heat transfer amount per unit area, from the relatively high-temperature seawater to the pipe wall in the second region A2, is suppressed. This prevents the occurrence of a temperature difference between LNG supplied to the vaporizingtube 21 adjacent to the second region A2 of the inlet-side header 22, and LNG supplied to the vaporizingtube 21 at a centermost position of the first region A1 of the inlet-side header 22. - Vaporized LNG, i.e., NG, from the vaporizing
tubes 21, is collected by the outlet-side header 24, and sent to the outlet-side manifold 19. The NG sent to the outlet-side manifold 19 is sent to a destination for consumption or the like, via the collectingpipe 14, and the pipe P2 connected to the outlet-side connection portion 14a. - As above, in the
vaporizer 10, even in a situation where seawater flowing down toward the second region A2 of the inlet-side header 22 has a temperature greater than that of seawater flowing down toward the first region A1 of the inlet-side header 22, the heat insulating member (heat-transfer suppressing section) 23 functions to suppress a heat transfer amount per unit area, from seawater to the overall second region A2 of the inlet-side header 22 (a region of the inlet-side header 22 inside the chamber H housing the vaporizing tube blocks 11, except the first region A1). Thus, it becomes possible to prevent a temperature in the second region A2 of the inlet-side header 22 from becoming greater than that in the first region A1 of the inlet-side header 22. This makes it possible to suppress a temperature difference between LNG distributed to the vaporizingtube 21 at an endmost position of the vaporizingtube panel 16 in the horizontal direction (width direction) thereof, and LNG distributed to the vaporizingtube 21 at a centermost position of the first region A1 in the horizontal direction. As a result, it becomes possible to prevent bending deformation of the inlet-side header 22 due to amounts of thermal expansion/shrinkage in the vaporizingtubes 21. - In the
vaporizer 10 according to this embodiment, the overall (entire) second region A2 of the inlet-side header 22 is surrounded by theheat insulating member 23. This makes it possible to suppress a heat transfer amount per unit area from seawater to the second region A2 of the inlet-side header 22, as compared to a heat transfer amount per unit area from seawater to the first region A1 of the inlet-side header 22, in an easy and reliable manner. - In the
vaporizer 10 according to this embodiment, theheat insulating member 23 has given stretchability, so that it becomes possible to prevent damage of theheat insulating member 23 due to thermal expansion/shrinkage of the inlet-side header 22. Specifically, the inlet-side header 22 thermally expands or shrinks due to a temperature difference between during operation of thevaporizer 10 and during stopping of thevaporizer 10. In this situation, theheat insulating member 23 surrounding the inlet-side header 22 has given stretchability, so that it can stretch or contract according to thermal expansion/shrinkage of the inlet-side header 22. This makes it possible to effectively prevent damage of theheat insulating member 23 due to thermal expansion/shrinkage (particularly, thermal expansion/shrinkage in the radial direction) of the inlet-side header 22. - In order to ascertain effects of the heat insulating member, by using a vaporizer having the same configuration as that of the
vaporizer 10, except theheat insulating member 23, a temperature of LNG flowing in the second region of the inlet-side header 22 during operation of the vaporizer was checked - An inlet-side header of this vaporizer is made of aluminum and formed to have an outer diameter of 165.2 mm. The inlet-side header has a heat transfer rate of 5000 W/mK. The heat insulating member has a heat conductivity of 1W/mK.
- A temperature of LNG flowing the second region of the above inlet-side header was measured while supplying LNG having a temperature of - 145°C, to the inlet-side header, under the following three conditions: without any heat insulating member; with a heat insulating member having a thickness of 0.5 mm; and with a heat insulating member having a thickness of 1.5 mm. A result of the measurement is illustrated in
FIG. 7 . - The graph in
FIG. 7 shows that a temperature rise of LNG flowing through the inlet-side header due to seawater can be suppressed by providing a heat insulating member on the second region of the inlet-side header even if the heat insulating member has a relatively small thickness, as compared to the case without any heat insulating member. - Based on this result, it was verified that a temperature difference between the first region and the second region in the inlet-side header can be suppressed by providing a heat insulating member on the second region, even in the situation where seawater flowing down toward the second region has a temperature greater than that of seawater flowing down toward the first region.
- The cryogenic liquid vaporizer of the present invention is not limited to the above embodiment, but it is to be understood that various changes and modifications may be made therein without departing from the scope thereof as set forth in appended claims
- A specific configuration of the
heat insulating member 23 is not particularly limited. For example, although theheat insulating member 23 in the above embodiment is formed by overlappingly winding (wrapping) a tape made of foamed plastic such as urethane foam, around the second region A2 of the inlet-side header 22, it is not limited thereto. That is, as illustrated inFIG. 8 , the heat insulating member may be tubular and bottomed tubular-shapedmembers heat insulating member 23A and the bottomed tubular-shapedheat insulating member 23B has an innerperipheral surface 123 with a diameter (inner diameter) corresponding to a diameter (outer diameter) of an outer peripheral surface of the second region A2 of the inlet-side header 22, or with an inner diameter greater than the outer diameter. The tubular-shapedheat insulating member 23A is fit on the second sub-region A2 of the inlet-side header 22 on the side of the inlet-side manifold 17. On the other hand, the bottomed tubular-shapedheat insulating member 23B is fit on the second sub-region A2 of the inlet-side header 22 on a side opposite to the inlet-side manifold 17. In this manner, the overall second region A2 is surrounded by the insulatingmembers - Alternatively, the heat insulating member may be formed by foamed plastic, such as urethane foam, sprayed onto the surface of the second region A2 of the inlet-
side header 22 to have a given thickness. - The heat-transfer suppressing section is not limited to the configuration surrounding the second region A2 of the inlet-
side header 22. For example, the heat-transfer suppressing section may be a cover member 60 (seeFIG. 9 ) disposed on an upper side of the second region A2 of the inlet-side header 22, and formed in a shape capable of covering over the second region A2 of the inlet-side header 22, in top plan view. Thiscover member 60 has a width (in a horizontal direction) greater than the outer diameter of the inlet-side header 22 so as to cover over the second region A2 of the inlet-side header 22, in top plan view. Further, thecover member 60 is disposed on the upper side of the second region A2 of the inlet-side header 22, in spaced-apart relation to (or in contact with) the second region A2. The above configuration can prevent seawater flowing down outside the vaporizing tube at the endmost position in the longitudinal direction of the inlet-side header (horizontal direction) and undergoing almost no heat exchange with LNG flowing through the vaporizing tube, from hitting against the second region of the inlet-side header. This makes it possible to prevent the occurrence of a temperature difference between the first region A1 and the second region A2 in the inlet-side header 22, even in the situation where seawater flowing down toward the second region A2 of the inlet-side header 22 has a temperature greater than that of seawater flowing down toward the first region A1 of the inlet-side header 22. That is, thecover member 60 is provided to prevent seawater falling down from theseawater supply section 30 from hitting against the second region A2 of the inlet-side header 22, so that it becomes possible to allow heat to become less likely to be transferred from the seawater to inside the second region A2 of the inlet-side header 22. In this manner, a temperature difference between LNG flowing through the first region A1 and LNG flowing through the second region A2 of the inlet-side header 22 may be suppressed. - Alternatively, the pipe wall of the second region A2 of the inlet-side header may be made of a material having a heat conductivity less than that of the pipe wall of the first region A1 of the inlet-side header. Specifically, for example, the pipe wall of the first region A1 may be made of a metal material having high heat conductivity, such as aluminum or an aluminum alloy, as with the first embodiment, and the pipe wall of the second region A2 may be made of iron or SUS. As a result, the heat conductivity in the pipe wall of the second region A2 of the inlet-side header becomes less than that in the pipe wall of the first region A1 of the inlet-side header. Thus, even when seawater having a temperature greater than that in the first region A1 hits against the second region A2, it becomes possible to prevent the occurrence of a temperature difference between LNG flowing through the first region A1 of the inlet-side header and LNG flowing through the second region A2 of the inlet-side header. This makes it possible to prevent bending deformation of the inlet-side header due to the above temperature difference.
- Further, only the pipe wall in the second region A2 of the inlet-
side header 22 may be formed in a layered structure in a thickness direction of the pipe wall. This configuration can suppress heat conductivity in a direction from s surface (outer peripheral surface) of the second region A2 of the inlet-side header to an inside of the second region A2 (inner peripheral surface of the inlet-side header), so that a heat conductivity (equivalent heat conductivity) of the pipe wall of the second region A2 of the inlet-side header 22 becomes less than that of the pipe wall of the first region A1 of the inlet-side header 22. Specifically, as illustrated inFIG. 10 , the pipe wall of the second region A2 of the inlet-side header 22 is composed of a plurality of layers (in the embodiments illustrated inFIG. 10 , two layers), and a heat-transfer suppressing layer 62 filled with air or a heat insulating material is formed between the layers. In this configuration, a heat conductivity (equivalent heat conductivity) in the pipe wall of the second region A2 of the inlet-side header 22 becomes less than that in the pipe wall of the first region A1 of the inlet-side header 22. The number of layers constituting the pipe wall may be three or more. - In the above embodiment, the header
inner pipe 50 is provided inside the inlet-side header 22. However, the vaporizer is not limited to this configuration. That is, the vaporizer may be configured to allow LNG to be directly supplied from the inlet-side manifold 17 to the inlet-side header 22, without providing the headerinner pipe 50. - As above, the cryogenic liquid vaporizer of the present invention is useful for vaporizing a cryogenic liquid, such as liquefied natural gas (LNG), liquefied petroleum gas (LPG) or liquid nitrogen (LN2), by means of heat exchange with a heat medium such as seawater, and suited to suppress bending deformation due to a difference in temperature of the inter-vaporizing tube distribution pipe in a longitudinal direction thereof.
Claims (6)
- A cryogenic liquid vaporizer (10) for vaporizing a cryogenic liquid, comprising:a vaporizing tube panel (16) including a plurality of vaporizing tubes (21) each extending in a vertical direction and for allowing the cryogenic liquid to flow therethrough so as to cause a heat exchange with an external medium, thereby vaporizing the cryogenic liquid, and an inter-vaporizing tube distribution pipe (22) for distributing the cryogenic liquid to the respective vaporizing tubes (21), wherein the plurality of vaporizing tubes (21) are arranged on a vertical plane and side-by-side in a horizontal direction, and the inter-vaporizing tube distribution pipe (22) is disposed to extend in the horizontal direction and connected to respective lower ends of the vaporizing tubes (21); anda liquid supply section (30) for supplying a heat-exchanging liquid from an upper end of the vaporizing tube panel (16) to allow the heat-exchanging liquid to flow down along the plurality of vaporizing tubes (21),characterized bya heat-transfer suppressing section (23) for suppressing a heat transfer amount per unit area from the heat-exchanging liquid to a second region (A2) of the inter-vaporizing tube distribution pipe (22) located outside a first region (A1) of the inter-vaporizing tube distribution pipe (22) in the horizontal direction, the first region (A1) being where the plurality of vaporizing tubes (21) are arranged and the heat-transfer suppressing section (23) being provided on only the second region (A2).
- The cryogenic liquid vaporizer (10) as defined in claim 1, wherein the heat-transfer suppressing section (23) is a heat insulating member (23) surrounding the second region (A2) of the inter-vaporizing tube distribution pipe (22), the heat insulating member (23) having a heat conductivity less than a heat conductivity of the inter-vaporizing tube distribution pipe (22).
- The cryogenic liquid vaporizer (10) as defined in claim 2, wherein the heat insulating member (23) has given stretchability.
- The cryogenic liquid vaporizer as defined in claim 1, wherein the heat-transfer suppressing section (23) is a cover member (60) which is disposed on an upper side of the second region (A2) of the inter-vaporizing tube distribution pipe (22), and formed in a shape capable of covering over the second region (A2) of the inter-vaporizing tube distribution pipe (22), in top plan view.
- The cryogenic liquid vaporizer (10) as defined in any one of claims 1 to 4, wherein a portion of the inter-vaporizing tube distribution pipe (22) between one end thereof and one of the vaporizing tubes (21) located on the side of the one end is disposed to penetrate through a partition wall (H1), wherein the second region (A2) is a region between the partition wall (H1) and the vaporizing tube (21) located on the side of the one end.
- A cryogenic liquid vaporizer for vaporizing a cryogenic liquid, comprising:a vaporizing tube panel (16) including a plurality of vaporizing tubes (21) each extending in a vertical direction and for allowing the cryogenic liquid to flow therethrough so as to cause a heat exchange with an external medium, thereby vaporizing the cryogenic liquid, and an inter-vaporizing tube distribution pipe (22) for distributing the cryogenic liquid to the respective vaporizing tubes (21), wherein the plurality of vaporizing tubes (21) are arranged on a specific vertical plane and side-by-side in a horizontal direction, and the inter-vaporizing tube distribution pipe (22) is disposed to extend in the horizontal direction and connected to respective lower ends of the vaporizing tubes (21); anda liquid supply section (30) for supplying a heat-exchanging liquid from an upper end of the vaporizing tube panel (16) to allow the heat-exchanging liquid to flow down along the plurality of vaporizing tubes (21),characterized in thatwith respect to a heat conductivity of a pipe wall in a first region (A1) of the inter-vaporizing tube distribution pipe (22) where the plurality of vaporizing tubes (21) are arranged, a heat conductivity of a pipe wall in a second region (A2) of the inter-vaporizing tube distribution pipe (22) located outside the first region (A1) in the horizontal direction has a smaller value.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2011052378A JP5714944B2 (en) | 2011-03-10 | 2011-03-10 | Low temperature liquefied gas vaporizer |
PCT/JP2011/007075 WO2012120580A1 (en) | 2011-03-10 | 2011-12-19 | Gasification device for low-temperature liquefied gas |
Publications (3)
Publication Number | Publication Date |
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EP2672213A1 EP2672213A1 (en) | 2013-12-11 |
EP2672213A4 EP2672213A4 (en) | 2015-03-04 |
EP2672213B1 true EP2672213B1 (en) | 2018-02-14 |
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EP11860385.1A Active EP2672213B1 (en) | 2011-03-10 | 2011-12-19 | Gasification device for low-temperature liquefied gas |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP2672213B1 (en) |
JP (1) | JP5714944B2 (en) |
KR (1) | KR101489114B1 (en) |
CN (1) | CN103403483B (en) |
WO (1) | WO2012120580A1 (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20140087219A (en) * | 2012-12-28 | 2014-07-09 | 재단법인 포항산업과학연구원 | High efficiency regenerator |
CN104089499B (en) * | 2014-06-27 | 2017-03-15 | 山东诺维科轻量化装备有限公司 | Liquified natural gas vaporizer and its production equipment and method |
CN104197189B (en) * | 2014-07-21 | 2017-06-30 | 中国科学院力学研究所 | A kind of liquid oxygen gasifier device |
JP6420223B2 (en) * | 2015-10-14 | 2018-11-07 | 株式会社神戸製鋼所 | Gas vaporizer |
CN106989630B (en) * | 2017-03-16 | 2018-12-25 | 上海交通大学 | A kind of piping and the large-scale ice chest with the piping structure |
CN110080846A (en) * | 2018-04-23 | 2019-08-02 | 江苏科技大学 | A kind of the monoblock type intermediate medium vaporizer and electricity generation system of band LNG cold energy use function |
JP6988035B2 (en) * | 2018-07-13 | 2022-01-05 | 株式会社三井E&Sマシナリー | Vaporizer |
JP6740289B2 (en) * | 2018-07-13 | 2020-08-12 | 株式会社三井E&Sマシナリー | Vaporizer |
CN112424464B (en) * | 2018-07-13 | 2021-07-06 | 三井易艾斯机械有限公司 | Gasifier |
CN108649470B (en) * | 2018-07-19 | 2024-01-26 | 珠海市伟名发展有限公司 | Explosion-proof case system based on cryogenic liquid pump |
JP7467028B2 (en) * | 2018-10-29 | 2024-04-15 | 株式会社神戸製鋼所 | Low-temperature liquefied gas vaporizer, cooling system, and method for suppressing ice formation in the vaporizer |
JP2020169783A (en) * | 2019-04-05 | 2020-10-15 | 株式会社神戸製鋼所 | Vaporizer and maintenance method of vaporizer |
WO2021081985A1 (en) * | 2019-11-01 | 2021-05-06 | Cryostar Sas | Vaporizer for vaporization of liquefied gases and method of vaporizing liquefied gas |
Family Cites Families (11)
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JPS5447706A (en) * | 1977-09-24 | 1979-04-14 | Osaka Gas Co Ltd | Equipment for gasifying liquefied gas of multi-components |
JPS5838677B2 (en) | 1980-09-20 | 1983-08-24 | 住友精密工業株式会社 | Open rack type vaporizer water sprinkler system |
JPH0648146B2 (en) * | 1990-03-30 | 1994-06-22 | 東京瓦斯株式会社 | Double pipe type open rack type vaporizer |
JPH04217788A (en) * | 1990-12-17 | 1992-08-07 | Kobe Steel Ltd | Vaporizer for liquefied natural gas |
JPH0626783A (en) * | 1992-07-10 | 1994-02-04 | Kobe Steel Ltd | Gasification device for liquefied natural gas |
JP3037073B2 (en) * | 1994-07-20 | 2000-04-24 | 株式会社神戸製鋼所 | Cryogenic liquid vaporizer |
JPH08183970A (en) | 1994-12-28 | 1996-07-16 | Tokyo Gas Co Ltd | Apparatus for preventing heat input of lower header in open rack type liquefied natural gas vaporizer |
JP3764956B2 (en) * | 1996-05-27 | 2006-04-12 | 住友精密工業株式会社 | Open rack type vaporizer |
JP3578693B2 (en) * | 1999-10-14 | 2004-10-20 | 株式会社コーアガス日本 | Air / hot water type gas production plant |
JP2007016968A (en) * | 2005-07-11 | 2007-01-25 | Kansai Electric Power Co Inc:The | Open rack type carburetor |
JP4796362B2 (en) * | 2005-09-13 | 2011-10-19 | 株式会社神戸製鋼所 | Heat transfer tube for LNG vaporizer and method for manufacturing the same |
-
2011
- 2011-03-10 JP JP2011052378A patent/JP5714944B2/en active Active
- 2011-12-19 WO PCT/JP2011/007075 patent/WO2012120580A1/en active Application Filing
- 2011-12-19 EP EP11860385.1A patent/EP2672213B1/en active Active
- 2011-12-19 CN CN201180068641.5A patent/CN103403483B/en active Active
- 2011-12-19 KR KR1020137026252A patent/KR101489114B1/en active IP Right Grant
Non-Patent Citations (1)
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Also Published As
Publication number | Publication date |
---|---|
JP5714944B2 (en) | 2015-05-07 |
CN103403483B (en) | 2015-09-09 |
EP2672213A1 (en) | 2013-12-11 |
CN103403483A (en) | 2013-11-20 |
KR101489114B1 (en) | 2015-02-02 |
EP2672213A4 (en) | 2015-03-04 |
KR20130132638A (en) | 2013-12-04 |
JP2012189125A (en) | 2012-10-04 |
WO2012120580A1 (en) | 2012-09-13 |
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