RU2016148615A - HEAT EXCHANGER WITH CHANNELS FOR DAMPING LIQUID MOVEMENTS - Google Patents

HEAT EXCHANGER WITH CHANNELS FOR DAMPING LIQUID MOVEMENTS Download PDF

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Publication number
RU2016148615A
RU2016148615A RU2016148615A RU2016148615A RU2016148615A RU 2016148615 A RU2016148615 A RU 2016148615A RU 2016148615 A RU2016148615 A RU 2016148615A RU 2016148615 A RU2016148615 A RU 2016148615A RU 2016148615 A RU2016148615 A RU 2016148615A
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Russia
Prior art keywords
heat exchanger
exchanger according
channels
casing
heat exchange
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RU2016148615A
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Russian (ru)
Inventor
Манфред ШТАЙНБАУЭР
Кристиане КЕРБЕР
Аксель ЛЕМАХЕР
Original Assignee
Линде Акциенгезелльшафт
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Publication of RU2016148615A publication Critical patent/RU2016148615A/en

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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)

Claims (17)

1. Теплообменник для опосредованного переноса тепла между первой средой (М1) и второй средой (М2), содержащий:1. A heat exchanger for indirect heat transfer between the first medium (M1) and the second medium (M2), comprising: - кожух (2), который имеет пространство (3) кожуха для размещения жидкой фазы (F1) первой среды (М1), и- a casing (2), which has a space (3) of the casing for accommodating the liquid phase (F1) of the first medium (M1), and - по меньшей мере один теплообменный блок (4), который имеет первые теплообменные проходы (Р) для приема первой среды (М1), а также вторые теплообменные проходы (Pʹ) для приема второй среды (М2), так что обеспечивается возможность опосредованного переноса тепла между обеими средами (М1, М2), при этом теплообменный блок (4) расположен в пространстве (3) кожуха так, что обеспечивается возможность его окружения находящейся в пространстве (3) кожуха жидкой фазой (F1) первой среды (М1),at least one heat exchange unit (4) that has first heat exchange passages (P) for receiving the first medium (M1), as well as second heat exchange passages (Pʹ) for receiving the second medium (M2), so that indirect heat transfer is possible between both media (M1, M2), while the heat exchange unit (4) is located in the space (3) of the casing so that it is possible to surround it with the liquid phase (F1) of the first medium (M1) in the space (3) of the casing, отличающийся тем, что в пространстве (3) кожуха сбоку по меньшей мере одного теплообменного блока (4, 5) предусмотрено множество проходящих параллельно друг другу цилиндрических каналов (10) для прохождения жидкой фазы (F1) первой среды (М1).characterized in that in the space (3) of the casing on the side of at least one heat exchange unit (4, 5), a plurality of cylindrical cylindrical channels (10) running parallel to each other are provided for passing the liquid phase (F1) of the first medium (M1). 2. Теплообменник по п. 1, отличающийся тем, что каналы (10) закреплены друг с другом так, что они образуют взаимосвязанный модуль (100), который, в частности, выполнен отдельно по меньшей мере от одного теплообменного блока (4) и/или кожуха (2).2. A heat exchanger according to claim 1, characterized in that the channels (10) are fixed to each other so that they form an interconnected module (100), which, in particular, is made separately from at least one heat exchange unit (4) and / or casing (2). 3. Теплообменник по п. 1 или 2, отличающийся тем, что длина каналов (10) вдоль продольной оси (L) соответствующего канала (10) больше, чем наибольший внутренний диаметр соответствующего канала (10) перпендикулярно соответствующей продольной оси.3. A heat exchanger according to claim 1 or 2, characterized in that the length of the channels (10) along the longitudinal axis (L) of the corresponding channel (10) is greater than the largest inner diameter of the corresponding channel (10) perpendicular to the corresponding longitudinal axis. 4. Теплообменник по п. 1 или 2, отличающийся тем, что каналы (10) относительно продольных осей (L) имеют одинаковую длину, или по меньшей мере некоторые каналы (10), в частности, для согласования модуля (100) с изогнутой зоной внутренней стороны (2а) кожуха (2) имеют относительно продольных осей (L) различные длины.4. A heat exchanger according to claim 1 or 2, characterized in that the channels (10) relative to the longitudinal axes (L) have the same length, or at least some channels (10), in particular, for matching the module (100) with a curved zone the inner side (2A) of the casing (2) have different lengths relative to the longitudinal axes (L). 5. Теплообменник по п. 1 или 2, отличающийся тем, что соответствующий канал (10) образован с помощью полого профиля (11), при этом, в частности, полые профили (11) соединены друг с другом так, что образуется взаимосвязанный модуль (100).5. A heat exchanger according to claim 1 or 2, characterized in that the corresponding channel (10) is formed using a hollow profile (11), while, in particular, the hollow profiles (11) are connected to each other so that an interconnected module ( one hundred). 6. Теплообменник по п. 1 или 2, отличающийся тем, что каналы (10) образованы с помощью множества соединенных друг с другом пластинчатых элементов, которые соединены друг с другом.6. A heat exchanger according to claim 1 or 2, characterized in that the channels (10) are formed by a plurality of plate elements connected to each other, which are connected to each other. 7. Теплообменник по п. 1 или 2, отличающийся тем, что продольные оси (L) каналов (10) проходят параллельно вертикали (z).7. The heat exchanger according to claim 1 or 2, characterized in that the longitudinal axis (L) of the channels (10) extend parallel to the vertical (z). 8. Теплообменник по п. 1 или 2, отличающийся тем, что продольные оси (L) каналов (10) проходят параллельно горизонтали.8. The heat exchanger according to claim 1 or 2, characterized in that the longitudinal axis (L) of the channels (10) extend parallel to the horizontal. 9. Теплообменник по п. 8, отличающийся тем, что по меньшей мере некоторые из каналов (10) имеют гидродинамический тормоз (12) потока или закрыты.9. A heat exchanger according to claim 8, characterized in that at least some of the channels (10) have a hydrodynamic flow brake (12) or are closed. 10. Теплообменник по п. 2, отличающийся тем, что модуль (100) имеет вдоль вертикали (z) длину, которая по меньшей мере больше половины высоты по меньшей мере одного теплообменного блока (4) вдоль вертикали (z), предпочтительно больше или равна высоте по меньшей мере одного теплообменного блока (4) вдоль вертикали (z).10. The heat exchanger according to claim 2, characterized in that the module (100) has a length along the vertical (z) that is at least more than half the height of at least one heat exchange unit (4) along the vertical (z), preferably greater than or equal to the height of at least one heat exchange unit (4) along the vertical (z). 11. Теплообменник по п. 2, отличающийся тем, что модуль (100) расположен по меньшей мере между одним теплообменным блоком (4) и соседним участком (2а) кожуха (2).11. A heat exchanger according to claim 2, characterized in that the module (100) is located between at least one heat exchange unit (4) and an adjacent portion (2a) of the casing (2). 12. Теплообменник по п. 1, отличающийся тем, что теплообменник (1) имеет дополнительный, расположенный в пространстве (3) кожуха теплообменный блок (5), который расположен вдоль горизонтали рядом с теплообменным блоком (4).12. A heat exchanger according to claim 1, characterized in that the heat exchanger (1) has an additional heat exchanger block (5) located in the space (3) of the casing, which is located along the horizontal next to the heat exchanger block (4). 13. Теплообменник по любому из пп. 2 или 12, отличающийся тем, что модуль (100) расположен между обоими теплообменными блоками (4, 5).13. The heat exchanger according to any one of paragraphs. 2 or 12, characterized in that the module (100) is located between the two heat exchange units (4, 5). 14. Теплообменник по п. 2, отличающийся тем, что теплообменник (1) имеет несколько модулей (100), каждый из которых имеет множество проходящих параллельно друг другу цилиндрических каналов (10) для прохождения жидкой фазы (F1) первой среды (М1), при этом, в частности, соответствующий модуль (100) расположен между одним из теплообменных блоков (4, 5) и соседним участком (2а) кожуха (2) или между двумя теплообменными блоками (4, 5).14. A heat exchanger according to claim 2, characterized in that the heat exchanger (1) has several modules (100), each of which has a plurality of cylindrical channels running parallel to each other (10) for passing the liquid phase (F1) of the first medium (M1), however, in particular, the corresponding module (100) is located between one of the heat exchange blocks (4, 5) and the adjacent section (2a) of the casing (2) or between two heat exchange blocks (4, 5).
RU2016148615A 2014-05-13 2015-05-07 HEAT EXCHANGER WITH CHANNELS FOR DAMPING LIQUID MOVEMENTS RU2016148615A (en)

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
RU2016148615A true RU2016148615A (en) 2018-06-13

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RU2016148615A RU2016148615A (en) 2014-05-13 2015-05-07 HEAT EXCHANGER WITH CHANNELS FOR DAMPING LIQUID MOVEMENTS

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)

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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

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FR2685071B1 (en) * 1991-12-11 1996-12-13 Air Liquide INDIRECT PLATE TYPE HEAT EXCHANGER.
US5651270A (en) * 1996-07-17 1997-07-29 Phillips Petroleum Company Core-in-shell heat exchangers for multistage compressors
DE19722360A1 (en) * 1997-05-28 1998-12-03 Bayer Ag Method and device for improving heat transfer
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
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WO2013096323A1 (en) * 2011-12-20 2013-06-27 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
CN106461348A (en) 2017-02-22
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

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