CN106461348A - Heat exchanger having channels for damping liquid motions - Google Patents
Heat exchanger having channels for damping liquid motions Download PDFInfo
- Publication number
- CN106461348A CN106461348A CN201580024722.3A CN201580024722A CN106461348A CN 106461348 A CN106461348 A CN 106461348A CN 201580024722 A CN201580024722 A CN 201580024722A CN 106461348 A CN106461348 A CN 106461348A
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- Prior art keywords
- heat exchanger
- passage
- medium
- block
- longitudinal axis
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- 239000007788 liquid Substances 0.000 title abstract description 16
- 230000033001 locomotion Effects 0.000 title abstract description 16
- 238000013016 damping Methods 0.000 title abstract 2
- 239000007791 liquid phase Substances 0.000 claims abstract description 38
- 239000011796 hollow space material Substances 0.000 claims description 13
- 238000005452 bending Methods 0.000 claims description 2
- 230000005540 biological transmission Effects 0.000 claims 1
- 239000012071 phase Substances 0.000 description 11
- 239000007789 gas Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 238000007667 floating Methods 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- 238000002309 gasification Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000004411 aluminium Substances 0.000 description 2
- 230000003466 anti-cipated effect Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
Classifications
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0017—Flooded core heat exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0262—Details of the cold heat exchange system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
- F25J1/0277—Offshore use, e.g. during shipping
- F25J1/0278—Unit being stationary, e.g. on floating barge or fixed platform
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
- F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
- F25J5/005—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger in a reboiler-condenser, e.g. within a column
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
-
- 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
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
-
- 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
- F28F9/005—Other auxiliary members within casings, e.g. internal filling means or sealing means
-
- 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
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/02—Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/20—Boiler-condenser with multiple exchanger cores in parallel or with multiple re-boiling or condensing streams
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/72—Processing device is used off-shore, e.g. on a platform or floating on a ship or barge
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0033—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for cryogenic applications
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0061—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
- F28D2021/0063—Condensers
-
- 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
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
- F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
- F28F2009/224—Longitudinal partitions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Ocean & Marine Engineering (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
The invention discloses a heat exchanger having channels for damping liquid motions. The invention relates to a heat exchanger (1) for indirect heat transfer between a first medium (M1) and a second medium (M2), comprising: a shell (2), which has a shell space (3) for accommodating a liquid phase (F1) of the first medium (M1), and at least one heat-exchanger block (4), which has first heat-transfer passages for accommodating the first medium (M1) and second heat-transfer passages for accommodating the second medium (M2), such that indirect heat can be transferred between the two media (M1, M2), wherein the at least one heat-exchanger block (4, 5) is arranged in the shell space (3) in such a way that the at least one heat-exchanger block can be surrounded with a liquid phase (F1) of the first medium (M1) located in the shell space (3). According to the invention, a plurality of cylindrical channels (10) extending parallel to each other for conducting the liquid phase of the first medium (M1) is provided in the shell space (3) laterally to the at least one heat-exchanger block (4).
Description
Technical field
The present invention relates to a kind of according to claim 1 for indirect heat transfer between the first medium and the second medium
Heat exchanger.
Background technology
Such heat exchanger generally has housing and at least one (also referred to as " core "), and this housing limits for receiving first
The shell space of the liquid phase of medium, described heat exchanger block has the first heat transfer path for receiving the first medium and is used for receiving
Second heat transfer path of the second medium, thus heat can transmit indirectly between two kinds of media, wherein heat exchanger block can with it
It is arranged in shell space by the mode of the liquid phase encirclement positioned at the first medium in shell space.
Such a heat exchanger is for example in " The standards of the brazed aluminium plate-fin
Heat exchanger manufacturer's association (ALPEMA) ", the third edition, 2010, Fig. 9 of page 67-
Shown in 1.This construction of heat exchanger is also referred to as " core shell formula (core-in-shell) " or " block shell-type (block-in-
Shell) " heat exchanger.
Preferably being produced by the thermosyphon effect that gasification causes makes the first medium (as cold-producing medium) pass through at least one heat exchanger
The driving force of block flowing.However, the shell space of heat exchanger not only executes the purpose of storage tank, and also serve as so that the first matchmaker
The steam of generation being situated between and the refrigerant liquid of the first medium or the segregation apparatuss of liquid phase separation.Therefore, in order to related to system
The reason, the Free Surface of the liquid phase of the first medium is formed in shell space.In this case, heat exchanger is preferably circle
By level and can be vertically provided for longitudinal axis that the housing of cylindrical form relates to or cylinder body axis.In principle, freeze
Agent liquid mainly flows upwardly through heat exchanger block.Especially, do not limit fluid (the second medium) to be cooled flows through direction.
If heat exchanger is arranged on mobile base, for example, it is arranged on floating body (such as ship), can have been brought some
Liquid in the problem producing with hydraulically full container known, especially container or shell space can move back and forth, from
And the multiple positions for example in shell space obtain time dependent liquid level.Thus, for example, heat exchanger block is in the first medium
Liquid phase in immersion depth can change, this for example may reduce biography heat availability.Therefore, it is necessary to suppression bath as much as possible
(bath) liquid motion is to the degree being able to ensure that safety and reliable operation.
Content of the invention
For this background, the purpose of the present invention therefore that provide a kind of heat exchanger starting mentioned type herein,
It can alleviate the problems referred to above.
This problem is solved by the heat exchanger with feature according to claim 1.
It thus provides multiple cylindrical channels for guiding the first medium, described cylindrical channel is in parallel to each other
Extend and be especially only dynamically connected with bath or liquid phase stream or bathe or liquid phase can flow through described cylindrical channel, described cylindrical shape
Passage is laterally arranged in described shell space with respect at least one heat exchanger block described.
Herein, implication on ordinary meaning for the cylindrical shape is the bottom section of cylinder (in this application for the horizontal stroke of passage
Cross section) can have any desired plane domain, it especially can be with circular (cylinder), rectangle, square, triangle
Shape or hexagonal mode are formed.In this case, by along not being located in the plane of plane domain and be preferably perpendicular to
The straight line of this plane domain or transverse cross-sectional area extension or the longitudinal axis move described plane domain and form corresponding cylinder.
Equally, preferably to pass through wall body separated from one another on their circumference for each passage, accurately for described wall body preferred
For the form of periphery wall body, the wall body especially completely enclosing.In the case of this completely enclosed wall body, in respective channel
In along passage longitudinal axis flowing medium can not enter (with respect to longitudinal axis transversely) adjacent passage.
It is possible to a passage, some passages or all passages and there is the single periphery wall body of themselves.Equally deposit
In such probability, that is, the wall body of passage also forms a part for the wall body of adjacency channel.This is readily adaptable for use in multiple logical
Road or all passages.
Based on the solution of the present invention, when there is the surge movement of heat exchanger, can advantageously make the shell space of heat exchanger
In the first medium liquid phase static.In this case, surge movement is especially appreciated that as such a motion, the i.e. longitudinal axis of housing
Its locus of line or cylinder body axis especially periodic variation or gradient are (such as due to being arranged in water body when heat exchanger
On floating body on when surge).
If (hereafter having such supposition) for the heat exchanger desirably arranged, passage is for example along perpendicular
Aligned, then in the during the operation of heat exchanger, liquid phase can exist in the effusion of the upper end of heat exchanger block and with respect to heat exchanger block
Transversely again pass through passage to back downward into.In this case, passage represents the flow resistance in horizontal direction, which inhibits the first matchmaker
Liquid phase the moving along horizontal direction being situated between.
In the case of passage horizontal orientation, during the surge movement of heat exchanger liquid phase in the channel may come
Backflow is dynamic, and passage equally plays the effect of flow resistance in the horizontal direction due to limited flow cross section, therefore suppresses the first matchmaker
The corresponding sports of the liquid phase being situated between.If the longitudinal axis of parallel channels are horizontally aligned, especially can suppress to be become by the inclination of longitudinal axis
The liquid motion that the surge movement changed causes.
In principle, at least one heat exchanger block described can be for being especially transferred to first from the second medium by heat indirectly
Any one of be possible to heat exchanger of medium.
However, heat exchanger block is preferably plate type heat exchanger.This plate type heat exchanger generally has multiple plates or piece, described many
Individual plate or piece are arranged parallel to each other and form the multiple heat transfer paths for medium included in heat transfer.Plate type heat exchanger
Preferred embodiment has multiple conductive structures, and it is for example, partly tortuous, especially ripple or folding, and the form of piece is (
Know for fin), these conductive structures are arranged between two parallel separating plates or the piece of plate type heat exchanger, plate-type heat-exchange
Two outermost layers of device are formed by cover plate.In like fashion, between each two separating plate or between separating plate and cover plate due to
The fin that is respectively arranged in centre and define multiple media can be by the parallel channels of its flowing or heat transfer path.Accordingly, it is capable to
Adjacent heat transfer path is conducted heat between the medium of flowing, heat transfer path referred to as first heat transfer distributing to the first medium is logical
Road, and distribute to heat transfer path correspondingly referred to as second heat transfer path of the second medium.
Between the adjacent separating plate of each two or between cover plate and adjacent separating plate, being preferably used for of side is set to
Close the terminal pole (being known as side lever) of corresponding heat transfer path.First heat transfer path along vertical curve up and down open wide and
Especially not by terminal rod seal, thus the liquid phase of the first medium can enter the first heat transfer path and can be in plate-type heat-exchange from below
The first heat transfer path is left as liquid phase and/or gas phase in the top of device.
Cover plate, separating plate, fin and side lever be preferably made of aluminium and for example in furnace brazing together with.Using having spray
The suitable collecting chamber (header) of mouth, the medium of for example, second medium can be introduced into the heat transfer path of distribution and from these heat transfers
Path is discharged.
The housing of heat exchanger especially can have periphery, (circular) columnar wall body, and described wall body is in heat exchanger on schedule
Preferably it is aligned in the following manner in the case of hoping arrangement, that is, the longitudinal axis (cylinder body axis) of described wall body or housing are along horizontal line
Or extend along vertical curve.On end face, housing preferably have relative to each other, connect to the wall body being previously mentioned and with respect to
Longitudinal axis or the wall of cylinder body axis horizontal expansion.
As for the operator scheme of heat exchanger, as explained at the beginning, it is preferably placed such that, i.e. at least one plate
Formula design of heat exchanger one-tenth exists with respect to the first medium cooling of guiding in adjacent first heat transfer path and/or at least part of liquefaction
In second heat transfer path, so that forming the gas phase of the first medium, described shell space is designed to receive the second medium of guiding
Collect described gas phase.
Further preferably so arrange, that is, at least one plate type heat exchanger is designed to the during the operation in heat exchanger, the first medium
At least one plate type heat exchanger rises, specifically in first heat transfer arranging for this purpose of at least one plate type heat exchanger
Rise in path, at least one plate type heat exchanger described is specifically configured to countercurrently or horizontal with the first medium in the second heat transfer path
The mode of stream guides the second medium.The liquid phase of the first medium leaving together with gas phase in the upper end of plate type heat exchanger can be perpendicular
Flow downward again in the side of plate type heat exchanger in the passage of straight orientation.
According to a preferred embodiment of the invention, so arrange, that is, passage or its wall body form the side of interconnecting unit with them
Formula interfixes, and this interconnecting unit is also referred to as labialpipe row (register).This unit is preferably by heat exchanger block and/or housing
It is individually formed.
In addition, according to a preferred embodiment of the invention, so arrange, that is, at least some of passage or passage passage is formed
It is respective longitudinal axis (cylinder body axis) longitudinal extension along them, be more than relatively along the development length of respective longitudinal axis
Maximum inner diameter in each vertical passage of respective longitudinal axis line.
Therefore, the liquid phase of the first medium can flow through passage along the respective longitudinal axis line of passage or cylinder body axis, and it is two
It is respectively provided with opening, liquid phase can enter and leave corresponding passage by described opening at each of individual end face.In this case,
Two openings of passage become state relative to each other along the longitudinal axis of respective channel or cylinder body axis, that is, be in always
Line.
According to a preferred embodiment of the invention, so arrange, that is, with respect to longitudinal axis, it is long that all passages have identical
Degree.Alternatively, the preferable configuration according to the present invention, is so arranged, that is, with respect to longitudinal axis, part or all of in passage
Passage has different length so that described unit is adapted to the bending area of the inner side of heat exchanger shell.This allows for multiple
Close the staged classification following inside region (for example in the case of hollow circle tube housing) profile in the outside of unit
(stepped graduation).
In principle, exist by the unit being arranged in shell space be fixed to housing may so that this unit especially not
Contact with least one heat exchanger block.Alternatively, described unit also can be fixed at least one heat exchanger block or be fixed to list
Only bearing part.
According to one kind construction of the present invention, particularly preferably so arrange, that is, each passage is formed by hollow material.Preferably by
The hollow material that metal (such as aluminum or steel) is made forms in this case and surrounds the wall body of each passage and thus define or shape
Become each passage.Hollow material is preferably connected with each other in the way of forming the interconnecting unit being previously mentioned.In this case, hollow type
Material can be welded to each other or is suitably fixed to one another by other fastener meanses, thus producing the unit being previously mentioned or hollow material pipe
Row.
According to another embodiment of the present invention, passage is formed by the plate element (such as piece) of multiple interconnection.These elements
It is formed as flat (such as flat sheet) or there is a kind of structure (element being for example previously mentioned is formed as on cross section
Ripple or folding or step-like or jagged element/piece).Each element for example can be by loading and phase each other
Mutually fix, and may additionally mutually fasten.In order to realize fixing or fasten.It is contemplated that soldering and/or be welded to connect, riveting
Nail connects or other frictional engagement interlocking and/or material bonding connection.
According to a preferred embodiment of the invention, so arrange, that is, also relative to it is anticipated that the heat exchanger arranged, passage
Longitudinal axis parallel to vertical curve extend.In this case, for horizontal type shell, the longitudinal axis of passage can be with respect to housing
Longitudinal axis or cylinder extend perpendicularly to the axis.For vertical shell, the longitudinal axis of Vertical Channel are preferably parallel to shell
The longitudinal axis of body or cylinder body axis extend.
According to the alternative preferred embodiment of the present invention, so arrange, that is, also relative to it is anticipated that the heat exchange arranged
Device, the longitudinal axis of passage extend parallel to horizontal line.In this case, for horizontal type shell, the longitudinal axis of passage can be put down
Row extends in the longitudinal axis of housing or cylinder body axis.For vertical shell, the longitudinal axis of horizontal channel preferably with respect to
The longitudinal axis of housing or cylinder extend perpendicularly to the axis.
According to a preferred embodiment of the invention, also so arrange, that is, for horizontal-extending passage, in described passage extremely
Some passages few have flow blockage part or closure, thus producing specific effect to liquid phase.
According to a preferred embodiment of the invention, also so arrange, i.e. described unit or possible passage, along vertical curve
Length at least above at least one plate type heat exchanger described or heat exchanger block along the height of vertical curve half, preferably greater than or
Equal at least one plate type heat exchanger described or heat exchanger block along vertical curve height.
Can also so arrange for horizontal channel, that is, horizontal channel is shorter than in the same direction on its longitudinal axis
The length of the heat exchanger block of possible lateral arrangement.
At least one heat exchanger block and housing or housing are preferably placed in by the unit that multiple passages or hollow material are made
And the part of described piece of level of relative or inside region between.
If multiple separate heat exchanger blocks are arranged in shell space, described unit may also be arranged on two such piece
Between.
Finally, under a heat exchanger block and multiple heat exchanger block both of these case, can arrange and each there are multiple passages
Multiple units, subsequent unit is preferably placed between one of heat exchanger block heat exchanger block and housing (as described above)
Or be arranged between two adjacent heat exchange device blocks.
In such a case it is possible to manner described above design unit.Other heat exchanger block preferably designs successively
Become plate type heat exchanger, be specifically configured to above-described form.
Brief description
Description by the accompanying drawing to exemplary embodiment below based on accompanying drawing is entered by the other details of the present invention and advantage
Row is explained.Also the clear stipulaties advantageous embodiment of the present invention in claims.
In the accompanying drawings：
Fig. 1 is the show in schematic partial sections of the heat exchanger with vertical shell and Vertical Channel according to the present invention；
Fig. 2 is the plane graph of the detail view of Vertical Channel shown in Fig. 1；
Fig. 3 is the schematic partial section of another heat exchanger with horizontal type shell and Vertical Channel according to the present invention
Figure；
Fig. 4 is the show in schematic partial sections of the heat exchanger with vertical shell and horizontal channel according to the present invention；
Fig. 5 is the plane graph of the detail view of horizontal channel shown in Fig. 4；
Fig. 6 is the schematic partial section of another heat exchanger with horizontal type shell and horizontal channel according to the present invention
Figure；And
Fig. 7 is showing of two heat transfer paths of the plate type heat exchanger of the embodiment that for example can be used for Fig. 1, Fig. 3, Fig. 4 and Fig. 6
Meaning property sectional view.
Specific embodiment
Fig. 1 shows there is upright, preferably (circular) cylindrical shell 2 heat exchanger 1 together with Fig. 2, and described housing limits
Determine the shell space 3 of heat exchanger 1.In this case, housing 2 has periphery, columnar wall body 14, and this wall body is in end
Defined by two walls 15 relative to each other.The longitudinal axis of housing 2 or cylinder body axis are overlapped with vertical curve z.
In the present embodiment, deposit in the shell space 3 being surrounded by housing 2 and be arranged on two levels to be closely adjacent to each other
Heat exchanger block 4,5, described heat exchanger block is to have multiple parallel heat transfer path P, P ' plate type heat exchanger 4,5 of (with reference to Fig. 7).
In the present embodiment, each plate type heat exchanger 4,5 has multiple can be the conductive structure 41 of piece, and described in horizontal stroke
Be formed as on section tortuous that is to say, that for example, ripple, jagged or there is rectangular profile.These structures 41 are also claimed
Make fin 41 and be arranged between two flat separating plates or the piece 40 of plate type heat exchanger 4,5.By this way, every
Between two separating plates 40, (or between separating plate and cover plate, see below description) forms multiple parallel channels or forms heat transfer
Path P, P ', corresponding medium M1, M2 can flow through described parallel channels or heat transfer path.Two outermost layers 40 are by plate type heat exchanger
4th, 5 cover plate is formed, and between the adjacent separating plate of each two or separation cover plate 40, there is the terminal pole arranging side
42.Fig. 7 by example with detail view show by fin 41 and two adjacent separating plates 40 formed for the first medium M1
The first heat transfer path P and same by fin 41 and two adjacent separating plates 40 formed for adjacent the of the second medium M2
Two heat transfer path P '.Repeat this arrangement of path so that multiple first and second pass preferably in each plate type heat exchanger 4,5
Heat passage P, P ' arrange with being immediately adjacent to each other in an alternating manner.
In heat exchanger 1 during the operation, shell space 3 is filled with the first medium M1.This of entrance heat exchanger 1 circulates often
For biphase but it is also possible to only liquid.Subsequently, liquid phase F1 of the first medium M1 forms the bath surrounding plate type heat exchanger 4,5, the
Gas phase G1 of one medium M1 is in shell space 3 upper area (this gas phase can be discharged at this upper area) above liquid phase F1
Assemble.
Liquid phase F1 of the first medium M1 rises in the first heat transfer path P of plate type heat exchanger 4,5, and is passed due to indirect
Heat and by the second medium M2 partial gasification to be cooled, the second medium M2 is in the second heat transfer path P ' of plate type heat exchanger 4,5
For example it is directed in the way of crossing current (cross-flow) with respect to the first medium M1.The gas phase of consequent first medium M1
G1 can leave in the upper end of plate type heat exchanger 4,5 and discharge from shell space 3 above block 4,5.One of liquid phase F1
Point continue in shell space 3 circulate, this part being previously mentioned in plate type heat exchanger 4,5 in the first heat transfer path P the bottom of from
Portion transmits upwards, subsequently flows down to the outside of the plate type heat exchanger 4,5 in shell space 3 again.
Second medium M2 is imported in plate type heat exchanger 4,5, and after flowing through the second distributed heat transfer path P ' with
Cooling or liquefied form are discharged from plate type heat exchanger 4,5.
Subsequently, in order to when there is surge movement in housing 2 (longitudinal axis or cylinder body axis fluctuate around vertical curve z) make shell
Liquid phase F1 in body space 3 is static, is provided with three units 100 as shown in Figure 1, and each unit has multiple parallel channels 10,
Described parallel channels extend respectively along the longitudinal axis L of the longitudinal axis z parallel to housing 2.According to Fig. 2, these passages 10 are preferred
Formed, for example, defined circle-cylindrical channel 10 and exist simultaneously by multiple hollow materials 11 being suitably connected to each other
Each end of both sides has opening 10a, 10b, and one of opening 10a is disposed generally on upward and along vertical curve z
At the height of upper end of corresponding plate type heat exchanger 4,5, and another contrary opening 10b exists respectively down and along vertical curve z
The lower section of block 4,5 terminates.Passage 10 is arranged to close to each other preferably along two orthogonal direction in spaces.
Then, Vertical Channel 10 allows liquid phase F1 just leaving corresponding plate type heat exchanger 4,5 in upper end from the first path P again
Secondary subsequently enter the first heat transfer path P in the lower end of plate type heat exchanger 4,5 in liquid phase F1 herein to bottom cycle, and due to
Thermosyphon effect is attracted again up, thus by partial gasification and cool down the second medium M2.
In this embodiment, Vertical Channel 10 represents the flow resistance in horizontal direction, and therefore suppresses the liquid of the first medium M1
The respective horizontal motion of phase F1, and protect the Verticle circulating by passage 10 being previously mentioned simultaneously.
According to Fig. 1, in unit 100, a unit between two plate type heat exchangers 4,5 is lateral with respect to two blocks 4,5
Ground arrangement.Two other units 100 are arranged in the horizontally adjacent of the periphery wall body 14 of plate type heat exchanger 4,5 and housing 2
Between part or inside region 2a.
Fig. 3 shows the modification of the heat exchanger 1 according to Fig. 1, and it is there is horizontal, longitudinal prolonging with the difference of Fig. 1
The housing 2 stretched, this housing is extended along the longitudinal axis being overlapped with horizontal line or cylinder body axis, that is, vertical with respect to vertical curve z
Ground extends.Different from Fig. 1, herein two plate type heat exchangers 4,5 along the longitudinal axis one of housing 2 in another rear ground cloth
Put, unit 100 side joint that two blocks 4,5 are each laterally designed by manner described above on both sides, described unit 100 edge
The longitudinal axis housing 2 distinguish two blocks of side joint 4,5 on the whole pattern length of two blocks 4,5.
Fig. 4 shows another modification of the heat exchanger 1 according to Fig. 1, and it is passage 10 flatly with the difference of Fig. 1
Extend that is to say, that the longitudinal axis that overlap with vertical curve z with respect to vertical shell 2 extend.Then, the opening of passage 10
Mouth 10a, 10b difference direction in the horizontal direction.According to Fig. 1, unit 100 is arranged with respect to plate type heat exchanger 4,5, two blocks 4,
Unit 100 between 5 has the passage 10 with bigger cross-sectional flow area compared to the unit 100 in the outside in block 4,5.Institute
Unit 100 is had to protrude past the upper and lower end of plate type heat exchanger 4,5 along vertical curve z, thus when heat exchanger 1 has surge movement
When make as much as possible the first medium M1 liquid phase F1 whole filling level remains stationary, according to Fig. 4's in this surge movement
The longitudinal axis z of housing 2 changes its gradient, particularly to the outside of paper plane.In this embodiment, existed by liquid phase F1
In horizontal channel, the flow resistance of experience, such as, when flowing back and forth between opening 10a, 10b of passage 10, create static.According to
Fig. 4, passage 10 or unit 100 can be formed with the hollow material that multiple cross sections are rectangular or square or by assembling each other or
Mutually the plate element of fastening, especially piece (seeing above) are formed.According to Fig. 5, Vertical Channel 10 is not only as the embodiment of Fig. 4
Rectangle is formed as shown on cross section, and can be circle.Other forms are equally contemplated that.In order to
Increase the flow resistance in horizontal direction, each horizontal channel 10 can be provided with the additional flow blockage part (obstruction on such as cross section
Thing) 12 or be completely enclosed.
Last Fig. 6 shows the heat exchanger 1 with horizontal channel 10 according to the mode of Fig. 4, and now the housing 2 of heat exchanger is pressed
Mode according to Fig. 3 forms and is arranged to horizontal.In this embodiment, in being placed according to Fig. 3 at another rear
Arrangement plate type heat exchanger 4,5 both sides, every kind of in the case of all in the level phase of each block 4,5 and the periphery wall body 14 of housing 2
Between adjacent inside region or part, setting has the unit 100 of multiple horizontal channels 10, and these horizontal channels one are arranged in separately
On one and close to each other, but the development length of the longitudinal axis along housing 2 for the horizontal channel is less than block 3,4 along the direction
Development length.This allows the Verticle circulating of liquid phase F1 to there is minimum possible disturbance (seeing above).According to Fig. 6, another unit
100 are arranged between two blocks 4,5 also along the longitudinal axis of housing 2.Herein, equally in the way of above based on described by Fig. 4
Realize the first medium liquid phase F1 static.
In principle, (or each) hollow material 11 of interconnection or passage 10 can with different cross-sectional form (for example
Circle, rectangle, honeycombed) and length be arranged on any position of the shell space 3 not occupied by each plate type heat exchanger 4,5,
And mainly fill region (i.e. near block 4 or 5, block 4 and 5 and/or between block 4 and 5) in liquid.Unit or pipe row 100
Quantity is adaptable.Only by these units 100 are flow through on liquid phase F1 in the vertical direction or horizontal mode.This assembly generation itself
Flow resistance in table horizontal direction.Therefore it is suppressed that bottom horizontal flow sheet.Unit 100 or passage 10 are in vertical size and horizontal size
On be all adaptable to various requirement, and also may be divided again.The cross sectional dimensions of each passage 10 are flexible, and equally
Adapt in various requirement.Each passage 10 of unit 100 can have different length.Especially in horizontal channel 10 or hollow type
In the case of material 11, in order to be adapted to flow resistance, each section bar 11 can be closed.Therefore it is suppressed that bottom horizontal flow sheet.
In a word, the unit according to the present invention or hollow material pipe row 100 allow the flowing to circulating liquid F1 in container 2
Direction applies big impact, without for this set much individual separate part.Liquid bulk outside plate type heat exchanger 4,5
Long-pending can be divided to a great extent, but the production being carried out by this and assembling spend and remain relatively low.This segmentation
Also unit 100 or passage 10/ hollow material 11 is allowed to have little wall thickness, this is because assembly 100 represents solid body 100
And only allow small-scale liquid motion.Be adapted to the size and assembly 100 of each element 10 size on the whole achieve right
The impact of natural frequency of vibration liquid F1 in container 2 or shell space 3 and the suppression to motion.Accordingly, it is capable to avoid certainly
So frequency excites and high amplitude.
It is particularly preferred that being used on the floating body on water body according to the heat exchanger 1 of the present invention, it is used for example as producing liquefaction
The part of the floating facility of natural gas (LNG).
Reference numerals list
| 1 | Heat exchanger |
| 2 | Housing |
| 2a | Inner side |
| 3 | Shell space |
| 4、5 | Plate type heat exchanger |
| 10 | Passage |
| 10a、10b | Opening |
| 11 | Hollow material |
| 14 | Wall body |
| 15 | Wall |
| 40 | Separating plate |
| 41 | Conductive structure or fin |
| 42 | Side lever |
| 100 | Unit |
| M1 | First medium |
| M2 | Second medium |
| G1 | The gas phase of the first medium |
| F1 | The liquid phase of the first medium |
| P | First heat transfer path |
| P’ | Second heat transfer path |
| Z | Vertical curve |
Claims (14)
1. a kind of heat exchanger, it is used for the indirect heat transfer between the first medium (M1) and the second medium (M2), described heat exchanger
Have：
Housing (2), it has the shell space (3) of the liquid phase (F1) for receiving described first medium (M1)；With
At least one heat exchanger block (4), it has the first heat transfer path (P) for receiving described first medium (M1) and is used for
Receive second heat transfer path (P ') of described second medium (M2) so that heat can be between described two media (M1, M2) between
Ground connection transmission, at least one heat exchanger block (4) wherein said can be by described first matchmaker in described shell space (3) with it
The mode that the liquid phase (F1) of Jie (M1) is surrounded is arranged in described shell space (3),
It is characterized in that,
With respect to described at least one heat exchanger block (4,5) on the side in the described shell space (3) arrangement multiple for
The cylindrical channel (10) guiding the liquid phase of described first medium (M1) and extending parallel to each other.
2. heat exchanger according to claim 1 is it is characterised in that described passage (10) forms interconnecting unit with them
(100) mode is fixed to one another, and described interconnecting unit is especially by least one heat exchanger block (4) described and/or described housing (2)
It is individually formed.
3. heat exchanger according to claim 1 and 2 is it is characterised in that described passage (10) is along each passage (10)
The development length of longitudinal axis (L) is more than the maximum inner diameter with respect to each longitudinal axis of each passage (10).
4. the heat exchanger according to one of aforementioned claim is it is characterised in that with respect to described longitudinal axis (L), described
Passage (10) has identical length, or with respect to described longitudinal axis (L), at least some passage (10) has different length
Degree, especially makes described unit (100) be adapted to the bending area of the inner side (2a) of described housing (2).
5. the heat exchanger according to one of aforementioned claim is it is characterised in that each passage (10) is by hollow material
(11) formed, especially by hollow material (11) shape interconnective in the way of the interconnecting unit (100) referring to described in being formed
Become.
6. the heat exchanger according to one of aforementioned claim is it is characterised in that described passage (10) is mutually interconnected by multiple
The interconnection plate element connecing is formed.
7. the heat exchanger according to one of aforementioned claim is it is characterised in that the longitudinal axis (L) of described passage (10) are put down
Row extends in vertical curve (z).
8. the heat exchanger according to one of claim 1 to 6 is it is characterised in that the longitudinal axis (L) of described passage (10) are put down
Row extends in horizontal line.
9. heat exchanger according to claim 8 is it is characterised in that at least some of described passage (10) passage has stream
Dynamic block piece (12) or (12) of closure.
10., according to claim 2 or according to returning the heat exchanger drawing described in one of claim 3 to 9 of claim 2, it is special
Levy and be, described unit (100) along described vertical curve (z) length at least above at least one heat exchanger block (4) edge described
The half of the height of described vertical curve (z), at least one heat exchanger block (4) preferably greater than or equal to described along described vertically
The height of line (z).
11. according to claim 2 or according to returning the heat exchanger drawing described in one of claim 3 to 10 of claim 2, and it is special
Levy and be, described unit (100) is arranged in the adjacent part (2a) of at least one heat exchanger block (4) described and described housing (2)
Between.
12. heat exchangers according to one of aforementioned claim are it is characterised in that described heat exchanger (1) has is arranged in
It is placed close to another heat exchanger of one heat exchanger block (4) in described shell space (3) and along described horizontal line
Block (5).
13. heat exchangers according to claim 2 and 12 are it is characterised in that described unit (100) is arranged in described two changing
Between hot device block (4,5).
14. heat exchangers according to one of aforementioned claim are it is characterised in that described heat exchanger (1) has multiple lists
First (100), described unit is respectively provided with multiple liquid phases (F1) for guiding described first medium (M1) and is parallel to each other
Cylindrical channel (10), especially unit (100) are arranged in one of described heat exchanger block (4,5) and described housing
(2) between adjacent part (2a) or be arranged between two heat exchanger blocks (4,5).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP14001684.1 | 2014-05-13 | ||
| EP14001684.1A EP2944909A1 (en) | 2014-05-13 | 2014-05-13 | Heat exchanger with channels for damping movements of liquids |
| PCT/EP2015/000931 WO2015172870A1 (en) | 2014-05-13 | 2015-05-07 | Heat exchanger having channels for damping liquid motions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106461348A true CN106461348A (en) | 2017-02-22 |
Family
ID=50729335
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201580024722.3A Pending CN106461348A (en) | 2014-05-13 | 2015-05-07 | Heat exchanger having channels for damping liquid motions |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US20170051985A1 (en) |
| EP (2) | EP2944909A1 (en) |
| JP (1) | JP2017519174A (en) |
| KR (1) | KR20170005092A (en) |
| CN (1) | CN106461348A (en) |
| AU (1) | AU2015258457A1 (en) |
| CA (1) | CA2947366A1 (en) |
| ES (1) | ES2657848T3 (en) |
| MX (1) | MX2016014435A (en) |
| RU (1) | RU2016148615A (en) |
| TR (1) | TR201802608T4 (en) |
| WO (1) | WO2015172870A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6904190B2 (en) * | 2017-09-19 | 2021-07-14 | 株式会社デンソー | Vehicle heat exchanger |
| US10823453B2 (en) * | 2017-11-20 | 2020-11-03 | Atlantic, Gulf & Pacific Company Of Manila, Inc. | Marinized vaporizer units, and methods of making and using same |
| US20220316646A1 (en) | 2019-11-15 | 2022-10-06 | Linde Gmbh | Transition component having insulation |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5651270A (en) * | 1996-07-17 | 1997-07-29 | Phillips Petroleum Company | Core-in-shell heat exchangers for multistage compressors |
| CN1200479A (en) * | 1997-05-28 | 1998-12-02 | 拜尔公司 | Method and apparatus for improving heat transfer |
| US20130153179A1 (en) * | 2011-12-20 | 2013-06-20 | Conocophillips Company | Internal baffle for suppressing slosh in a core-in-shell heat exchanger |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2922287A (en) * | 1954-03-22 | 1960-01-26 | Garrett Corp | Liquid storage tank |
| US4750631A (en) * | 1986-07-21 | 1988-06-14 | Sperry Corporation | Anti-slosh apparatus for liquid containers |
| FR2685071B1 (en) * | 1991-12-11 | 1996-12-13 | Air Liquide | INDIRECT PLATE TYPE HEAT EXCHANGER. |
| FR2807826B1 (en) * | 2000-04-13 | 2002-06-14 | Air Liquide | BATH TYPE CONDENSER VAPORIZER |
| KR101313617B1 (en) * | 2010-07-13 | 2013-10-02 | 삼성중공업 주식회사 | Sloshing impact reduce device of Cargo Containment and method of reduce the same |
| WO2012077143A1 (en) * | 2010-12-09 | 2012-06-14 | Provides Metalmeccanica S.R.L. | Heat exchanger |
| US9746256B2 (en) * | 2011-11-18 | 2017-08-29 | Carrier Corporation | Shell and tube heat exchanger with a vapor port |
-
2014
- 2014-05-13 EP EP14001684.1A patent/EP2944909A1/en not_active Withdrawn
-
2015
- 2015-05-07 RU RU2016148615A patent/RU2016148615A/en not_active Application Discontinuation
- 2015-05-07 CN CN201580024722.3A patent/CN106461348A/en active Pending
- 2015-05-07 ES ES15720913.1T patent/ES2657848T3/en active Active
- 2015-05-07 AU AU2015258457A patent/AU2015258457A1/en not_active Abandoned
- 2015-05-07 CA CA2947366A patent/CA2947366A1/en not_active Abandoned
- 2015-05-07 KR KR1020167034761A patent/KR20170005092A/en unknown
- 2015-05-07 TR TR2018/02608T patent/TR201802608T4/en unknown
- 2015-05-07 MX MX2016014435A patent/MX2016014435A/en unknown
- 2015-05-07 WO PCT/EP2015/000931 patent/WO2015172870A1/en active Application Filing
- 2015-05-07 EP EP15720913.1A patent/EP3143352B1/en active Active
- 2015-05-07 JP JP2016567663A patent/JP2017519174A/en active Pending
- 2015-05-07 US US15/308,113 patent/US20170051985A1/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5651270A (en) * | 1996-07-17 | 1997-07-29 | Phillips Petroleum Company | Core-in-shell heat exchangers for multistage compressors |
| WO1998002698A1 (en) * | 1996-07-17 | 1998-01-22 | Phillips Petroleum Company | Core-in-shell heat exchangers for multistage compressors |
| CN1200479A (en) * | 1997-05-28 | 1998-12-02 | 拜尔公司 | Method and apparatus for improving heat transfer |
| US20130153179A1 (en) * | 2011-12-20 | 2013-06-20 | Conocophillips Company | Internal baffle for suppressing slosh in a core-in-shell heat exchanger |
Also Published As
| Publication number | Publication date |
|---|---|
| MX2016014435A (en) | 2017-01-23 |
| ES2657848T3 (en) | 2018-03-07 |
| US20170051985A1 (en) | 2017-02-23 |
| EP2944909A1 (en) | 2015-11-18 |
| EP3143352A1 (en) | 2017-03-22 |
| JP2017519174A (en) | 2017-07-13 |
| WO2015172870A1 (en) | 2015-11-19 |
| KR20170005092A (en) | 2017-01-11 |
| TR201802608T4 (en) | 2018-03-21 |
| EP3143352B1 (en) | 2017-11-29 |
| CA2947366A1 (en) | 2015-11-19 |
| AU2015258457A1 (en) | 2016-11-10 |
| RU2016148615A (en) | 2018-06-13 |
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