EP2553370A2 - Device for the cryogenic separation of air - Google Patents
Device for the cryogenic separation of airInfo
- Publication number
- EP2553370A2 EP2553370A2 EP11714930A EP11714930A EP2553370A2 EP 2553370 A2 EP2553370 A2 EP 2553370A2 EP 11714930 A EP11714930 A EP 11714930A EP 11714930 A EP11714930 A EP 11714930A EP 2553370 A2 EP2553370 A2 EP 2553370A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- column
- mixing
- mixing column
- double
- coldbox
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 70
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000004821 distillation Methods 0.000 claims abstract description 4
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000001301 oxygen Substances 0.000 claims abstract 2
- 229910052760 oxygen Inorganic materials 0.000 claims abstract 2
- 201000009240 nasopharyngitis Diseases 0.000 abstract description 10
- 238000004781 supercooling Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 238000010276 construction Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000009835 boiling Methods 0.000 description 3
- 235000019362 perlite Nutrition 0.000 description 3
- 239000010451 perlite Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 241000883306 Huso huso Species 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/0446—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the heat generated by mixing two different phases
- F25J3/04466—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the heat generated by mixing two different phases for producing oxygen as a mixing column overhead gas by mixing gaseous air feed and liquid oxygen
-
- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
- F25J3/04872—Vertical layout of cold equipments within in the cold box, e.g. columns, heat exchangers etc.
-
- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
- F25J3/0489—Modularity and arrangement of parts of the air fractionation unit, in particular of the cold box, e.g. pre-fabrication, assembling and erection, dimensions, horizontal layout "plot"
-
- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
- F25J3/04945—Details of internal structure; insulation and housing of the cold box
-
- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/04—Processes or apparatus using separation by rectification in a dual pressure main column system
Definitions
- the invention relates to a device for the cryogenic separation of air according to the preamble of patent claim 1.
- a coldbox is used for the thermal insulation of plant components (see, for example, Hausen / Linde, Tiefftemperaturtechnik, 1985, in particular pages 490 and 491).
- a "cold box” is understood here as an insulating casing which has a
- Separation columns and / or heat exchangers Separation columns and / or heat exchangers.
- the insulating effect can be through
- a powdery material such as perlite is preferably used.
- the connecting elements can be made by any known technique, for example as profiles, tubes or a combination of such elements. They are preferably made of the same material as the column walls of mixing column and double column or of a similar material and are connected, for example by welding with these column walls. At the point of contact between connecting elements and column wall patches or reinforcing plates are preferably used, which consist of the same material as the column wall.
- the connecting elements are preferably made of metal profiles, which are also formed of the same material. If the common coldbox prefabricated in the factory and
- the connecting structure should be strong enough to absorb the forces from the horizontal transport.
- a frame construction made of Cr-Ni steel can be additionally attached to the paving sheet, which reinforces the construction, but also causes a relatively large distance between the columns.
- the mixing column is preferably not supported from below, but in particular is connected exclusively by the connecting elements with the double column. All information on the spatial orientation here refers to the orientation of the device during the operation of the columns.
- a container for example a column or a heat exchanger
- Upper edge (lower edge) of the other container is located. This may or may not be a vertical line passing through both containers. In the projection on a horizontal plane, the cross sections of the two containers may overlap, but they may also be arranged completely offset from one another. Analogously, the term "Germany'V'untrati" to understand.
- the main heat exchanger is arranged in the common cold box, so that the device has a total of only a single coldbox.
- the common cold box exceeds the permissible transport dimensions.
- the main heat exchanger is arranged in a further, separate from the common coldbox coldbox.
- the two cold boxes can be prefabricated in the workshop and then transported separately to the construction site.
- the device may also include a subcooling countercurrent.
- the subcooler countercurrent serves to subcool one or more liquids from one of the columns of the nitrogen-oxygen separation distillation column system or the mixing column in countercurrent to one or more cold gaseous streams, typically from the low pressure column to warm.
- liquid streams boiling at a higher pressure column e.g.
- the supercooling countercurrent can be arranged in a system with two cold boxes in the other coldbox.
- the supercooling countercurrent is placed in the common coldbox below the mixing column.
- the supercooling countercurrent is preferably arranged below the mixing column and is also with the
- Double column in particular connected to the high pressure column.
- the connection to the double column is realized by similar connecting elements as in the mixing column.
- the upper end of the double column is realized by similar connecting elements as in the mixing column.
- Mixing column arranged at least at the level of the upper end of the double column or at most one-fifth of the length of the double column below the upper end of the double column.
- the mixing column hangs as high as possible. Under certain conditions, it may even make sense to build the box higher than necessary for the double column in order to allow the transport of the bottom liquid from the mixing column in the low-pressure column without a pump.
- the additional steel construction costs can be outweighed by the saved pump costs. This applies in particular to a method with injection of turbine air into the mixing column, as shown, for example, in US Pat. No. 5,454,227 or US Pat. No. 5,490,391, the mixing column pressure being relatively low, in particular below that
- the mixing column can also be arranged lower.
- the upper ends of the mixing column and the double column are at the same geodetic height.
- the vertical distance between the upper end of the double column and the upper end of the mixing column is preferably 0.4 m to 7.0 m.
- the imaginary rectangle has at least one
- the base area of the common coldbox can be optimized. It should be noted that the narrow side of the cold box corresponds to the transport height, which must not exceed a maximum value for prefabricated cold boxes; the other side of the rectangle is the result and should otherwise be as small as possible. In the case of construction site assembly is the
- Figure 1 shows a first embodiment of the invention with an arrangement of
- FIG. 2 shows the first exemplary embodiment in vertical cross-section
- Figure 3 shows a second embodiment of the invention without supercooling countercurrent in the common coldbox
- Figure 4 shows the common coldbox of the second embodiment in vertical
- FIG. 1 Cross-sectional view.
- a mixing column 1 and a subcooling countercurrent 2 are arranged in a common coldbox 3.
- High-pressure column and low-pressure column of the distillation column system for nitrogen-oxygen separation are realized as a classic double column 5 and also housed in the common cold box 3.
- Figure 2 shows the same arrangement in another view.
- Bottom of the common cold box 3 is formed by a separate outer wall.
- the double column 5 is supported via a frame, not shown, on the bottom 4 of the common cold box 3.
- the mixing column 1 and the supercooling countercurrent are based on also not shown connecting elements on the double column 5 from. These connecting elements are the same or similar to the connecting elements shown in Figure 3 executed.
- a main heat exchanger is housed in the first embodiment in a separate further coldbox (not shown in Figures 1 and 2).
- the two dashed circles 1a and 1b in Figure 1 represent two modifications of the first embodiment, in which the mixing column is arranged offset to the supercooling countercurrent 2. However, the mixing column is also arranged above the supercooling countercurrent here (analogous to FIG. 2).
- the mixing column 1 and the double column 5 are arranged in the common coldbox 3.
- the subcooling countercurrent 2 is housed in another coldbox 12, together with the main heat exchanger 6.
- the main heat exchanger 6 is formed in the embodiment by a single heat exchanger block, in particular one
- Plate heat exchanger Alternatively, he can go through two or more horizontally
- FIG. 4 shows the same common coldbox in a different view.
- the space between the apparatus 1, 2, 5 and the outer wall of the common cold box 3 is filled with perlite.
- Coldbox 3 is formed by a separate outer wall.
- the double column 5 is supported on the bottom 4 of the common cold box 3 via a frame (frame), not shown.
- the mixing column 1 is supported exclusively on the double column 5, specifically via at least two connecting elements which are respectively arranged in the upper and lower region of the mixing column 1.
- the connecting elements are dimensioned accordingly, if necessary, more than two connecting elements can be used. In the illustrated
- Embodiment two pairs of connecting elements are used, which are each arranged in the upper and lower regions of the mixing column 1.
- the upper pair of these connecting elements 10, 11 is shown schematically in FIG.
- the upper element is designed as a fixed point (welded or screwed on both columns), the lower but as a guide bearing to
- This guide bearing fixes the horizontal arrangement and allows relative movement of mixing column and double column in the vertical direction.
- the roughly dashed line 14 in Figure 3 represents a thought rectangle, which has purely geometric meaning, but which corresponds to no part of the apparatus. (The space between the dashed line 14 and the outer wall 3 of the box here marks the minimum insulation distance in which no cold component may be located.)
- the imaginary rectangle 14 is in the horizontal, is oriented parallel to the walls of the coldbox 3 and lies also on the outer walls of the two columns 1, 5 at.
- the mixing column 1 is preferably in a corner of this
- Rectangles 14 arranged, that is, it is touched by the rectangle 14 in two places. ( Figure 4 does not fully illustrate this aspect for illustrative reasons.)
- FIGS. 3 and 4 represent a modification of the first exemplary embodiment, in which the mixing column 1a is arranged differently.
- the upper end 24 of the mixing column is located 0.4 m below the upper end 15 of the double column 5 at a total height of the double column of about 35 m.
- the orientation of the two cold boxes to each other may be different from that shown in the drawings and depending on the spatial boundary conditions are arbitrary.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL11714930T PL2553370T3 (en) | 2010-03-26 | 2011-03-25 | Device for the cryogenic separation of air |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102010012920A DE102010012920A1 (en) | 2010-03-26 | 2010-03-26 | Apparatus for the cryogenic separation of air |
PCT/EP2011/001004 WO2011116871A2 (en) | 2010-03-26 | 2011-03-01 | Device for the cryogenic separation of air |
PCT/EP2011/001509 WO2011116981A2 (en) | 2010-03-26 | 2011-03-25 | Device for the cryogenic separation of air |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2553370A2 true EP2553370A2 (en) | 2013-02-06 |
EP2553370B1 EP2553370B1 (en) | 2019-05-15 |
Family
ID=46245691
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11714930.2A Active EP2553370B1 (en) | 2010-03-26 | 2011-03-25 | Device for the cryogenic separation of air |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2553370B1 (en) |
PL (1) | PL2553370T3 (en) |
WO (1) | WO2011116981A2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2015071501A3 (en) * | 2013-11-18 | 2015-08-27 | Linde Aktiengesellschaft | Cold-box apparatus and cold-box system |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5817327B2 (en) * | 2010-09-29 | 2015-11-18 | 東ソー株式会社 | Oxide sintered body, method for producing the same, oxide transparent conductive film obtained using the same, and solar cell |
DE102011015233A1 (en) | 2011-03-25 | 2012-09-27 | Linde Ag | Apparatus for the cryogenic separation of air |
DE102012006484A1 (en) * | 2012-03-29 | 2013-10-02 | Linde Aktiengesellschaft | Transportable package with a coldbox and method of manufacturing a cryogenic air separation plant |
FR3119884B1 (en) * | 2021-02-18 | 2022-12-30 | Air Liquide | Air separation process by cryogenic distillation |
FR3123113B1 (en) * | 2021-05-19 | 2023-06-09 | Air Liquide | Distillation column and method of transporting a distillation column |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
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IT961138B (en) | 1971-02-01 | 1973-12-10 | Air Liquide | PLANT FOR COMPRESSING A FLUID BY EXPANSION OF ANOTHER FLUID |
US5454227A (en) | 1994-08-17 | 1995-10-03 | The Boc Group, Inc. | Air separation method and apparatus |
US5490391A (en) | 1994-08-25 | 1996-02-13 | The Boc Group, Inc. | Method and apparatus for producing oxygen |
DE19803437A1 (en) | 1998-01-29 | 1999-03-18 | Linde Ag | Oxygen and nitrogen extracted by low-temperature fractional distillation |
FR2774752B1 (en) | 1998-02-06 | 2000-06-16 | Air Liquide | AIR DISTILLATION SYSTEM AND CORRESPONDING COLD BOX |
FR2778233B1 (en) | 1998-04-30 | 2000-06-02 | Air Liquide | AIR DISTILLATION SYSTEM AND CORRESPONDING COLD BOX |
FR2778234B1 (en) | 1998-04-30 | 2000-06-02 | Air Liquide | AIR DISTILLATION SYSTEM AND CORRESPONDING COLD BOX |
US6134915A (en) * | 1999-03-30 | 2000-10-24 | The Boc Group, Inc. | Distillation column arrangement for air separation plant |
DE19951521A1 (en) | 1999-10-26 | 2001-05-03 | Linde Ag | Recovering pressurized product by low temperature decomposition of air in rectification system comprises cold compressing heat carrier stream before introducing into mixing column |
DE10015602A1 (en) | 2000-03-29 | 2001-10-04 | Linde Ag | Method and device for obtaining a printed product by low-temperature separation of air |
DE10139727A1 (en) | 2001-08-13 | 2003-02-27 | Linde Ag | Method and device for obtaining a printed product by low-temperature separation of air |
DE10161584A1 (en) * | 2001-12-14 | 2003-06-26 | Linde Ag | Device and method for generating gaseous oxygen under increased pressure |
DE10209421A1 (en) | 2002-03-05 | 2003-04-03 | Linde Ag | Process for recovering a compressed product comprises subjecting air to low temperature decomposition in a rectification system consisting of a high pressure column and a low pressure column |
DE10217093A1 (en) | 2002-04-17 | 2003-01-23 | Linde Ag | Separation column system, for separation of high purity nitrogen or oxygen, has temperature measurements at high pressure column and mixer column to set purity according to temperature |
DE10228111A1 (en) | 2002-06-24 | 2004-01-15 | Linde Ag | Air separation process and plant with mixing column and krypton-xenon extraction |
EP1387136A1 (en) | 2002-08-02 | 2004-02-04 | Linde AG | Process and device for producing impure oxygen by cryogenic air distillation |
GB0307404D0 (en) * | 2003-03-31 | 2003-05-07 | Air Prod & Chem | Apparatus for cryogenic air distillation |
EP1666824A1 (en) | 2004-12-03 | 2006-06-07 | Linde Aktiengesellschaft | Process and device for the recovery of Argon by cryogenic separation of air |
US7621152B2 (en) * | 2006-02-24 | 2009-11-24 | Praxair Technology, Inc. | Compact cryogenic plant |
DE102010012920A1 (en) * | 2010-03-26 | 2011-09-29 | Linde Aktiengesellschaft | Apparatus for the cryogenic separation of air |
-
2011
- 2011-03-25 WO PCT/EP2011/001509 patent/WO2011116981A2/en active Application Filing
- 2011-03-25 PL PL11714930T patent/PL2553370T3/en unknown
- 2011-03-25 EP EP11714930.2A patent/EP2553370B1/en active Active
Non-Patent Citations (1)
Title |
---|
See references of WO2011116981A2 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2015071501A3 (en) * | 2013-11-18 | 2015-08-27 | Linde Aktiengesellschaft | Cold-box apparatus and cold-box system |
US10145514B2 (en) | 2013-11-18 | 2018-12-04 | Man Energy Solutions Se | Cold-box system and method for power management aboard ships |
EP3071875B1 (en) * | 2013-11-18 | 2019-07-03 | MAN Energy Solutions SE | Cold-box apparatus and cold-box system |
US11118734B2 (en) | 2013-11-18 | 2021-09-14 | Man Energy Solutions Se | Cold-box system and apparatus for power management aboard ships |
Also Published As
Publication number | Publication date |
---|---|
WO2011116981A3 (en) | 2012-08-30 |
PL2553370T3 (en) | 2019-11-29 |
EP2553370B1 (en) | 2019-05-15 |
WO2011116981A2 (en) | 2011-09-29 |
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