DK200000939A - Proceskomponenter, beholdere og rør, der er velegnede til at indeholde og transportere fluider ved kryogene temperaturer - Google Patents
Proceskomponenter, beholdere og rør, der er velegnede til at indeholde og transportere fluider ved kryogene temperaturer Download PDFInfo
- Publication number
- DK200000939A DK200000939A DK200000939A DKPA200000939A DK200000939A DK 200000939 A DK200000939 A DK 200000939A DK 200000939 A DK200000939 A DK 200000939A DK PA200000939 A DKPA200000939 A DK PA200000939A DK 200000939 A DK200000939 A DK 200000939A
- Authority
- DK
- Denmark
- Prior art keywords
- approx
- pressure
- psia
- kpa
- temperature
- Prior art date
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- 239000012530 fluid Substances 0.000 title description 19
- 238000000034 method Methods 0.000 title description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 32
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 28
- 239000000463 material Substances 0.000 description 18
- DBIMSKIDWWYXJV-UHFFFAOYSA-L [dibutyl(trifluoromethylsulfonyloxy)stannyl] trifluoromethanesulfonate Chemical compound CCCC[Sn](CCCC)(OS(=O)(=O)C(F)(F)F)OS(=O)(=O)C(F)(F)F DBIMSKIDWWYXJV-UHFFFAOYSA-L 0.000 description 16
- 229910052759 nickel Inorganic materials 0.000 description 16
- 229910000922 High-strength low-alloy steel Inorganic materials 0.000 description 15
- 239000003345 natural gas Substances 0.000 description 14
- 230000008020 evaporation Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 239000003990 capacitor Substances 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
Classifications
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- 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
- F25J3/0295—Start-up or control of the process; Details of the apparatus used, e.g. sieve plates, packings
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- 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
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B19/00—Machines, plants or systems, using evaporation of a refrigerant but without recovery of the vapour
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/04—Ferrous alloys, e.g. steel alloys containing manganese
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/08—Ferrous alloys, e.g. steel alloys containing nickel
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/12—Ferrous alloys, e.g. steel alloys containing tungsten, tantalum, molybdenum, vanadium, or niobium
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/14—Ferrous alloys, e.g. steel alloys containing titanium or zirconium
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
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- C22C38/16—Ferrous alloys, e.g. steel alloys containing copper
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
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- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/40—Ferrous alloys, e.g. steel alloys containing chromium with nickel
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/40—Ferrous alloys, e.g. steel alloys containing chromium with nickel
- C22C38/42—Ferrous alloys, e.g. steel alloys containing chromium with nickel with copper
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- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
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- F04B15/06—Pumps adapted to handle specific fluids, e.g. by selection of specific materials for pumps or pump parts for liquids near their boiling point, e.g. under subnormal pressure
- F04B15/08—Pumps adapted to handle specific fluids, e.g. by selection of specific materials for pumps or pump parts for liquids near their boiling point, e.g. under subnormal pressure the liquids having low boiling points
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- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B23/00—Pumping installations or systems
- F04B23/02—Pumping installations or systems having reservoirs
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- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/02—Selection of particular materials
- F04D29/026—Selection of particular materials especially adapted for liquid pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C1/00—Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
- F17C1/14—Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge constructed of aluminium; constructed of non-magnetic steel
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- F17C13/00—Details of vessels or of the filling or discharging of vessels
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- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/08—Pipe-line systems for liquids or viscous products
- F17D1/082—Pipe-line systems for liquids or viscous products for cold fluids, e.g. liquefied gas
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- 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
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- 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
- F25J1/0203—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 using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle
- F25J1/0204—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 using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle as a single flow SCR cycle
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- 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
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- 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
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- 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
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- F25J1/0264—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
- F25J1/0265—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer
- F25J1/0268—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer using a dedicated refrigeration means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- C—CHEMISTRY; METALLURGY
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- C—CHEMISTRY; METALLURGY
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- C—CHEMISTRY; METALLURGY
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- 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
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead gas
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- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
-
- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/02—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams using a pump in general or hydrostatic pressure increase
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- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
-
- 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
- F25J2290/42—Modularity, pre-fabrication of modules, assembling and erection, horizontal layout, i.e. plot plan, and vertical arrangement of parts of the cryogenic unit, e.g. of the cold box
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- 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
- F25J2290/44—Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/902—Apparatus
- Y10S62/905—Column
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Water Supply & Treatment (AREA)
- Heat Treatment Of Steel (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Rigid Pipes And Flexible Pipes (AREA)
- Heat Treatment Of Articles (AREA)
- Thermal Insulation (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Laminated Bodies (AREA)
- Pressure Welding/Diffusion-Bonding (AREA)
Description
PATENTKRAV 1. Varmevekslersystem, der omfatter: (a) et varmevekslerlegeme, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end -40°C (-40°F), hvilket varmevekslerlegeme er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) en flerhed af ledeplader. 2. Varmevekslersystem, der omfatter: (a) varmevekslerlegeme, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilket varmevekslerlegeme er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) en flerhed af ledeplader. 3. Kondensatorsystem, der omfatter: (a) en kondensatorbeholder, der er velegnet til at indeholde et fluid ved et tryk, der er højere end 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilken kondensatorbeholder er konstrueret ved sammenføjning afen flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det undertryk stående fluid, og (b) vamevekslerorganer. 4. Fordampningssystem, der omfatter: (a) en fordampningsbeholder, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilken fordampningsbeholder er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) vamevekslerorganer. 5. Separatorsystem, der omfatter: (a) en separatorbeholder, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilken separatorbeholder er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) mindst én isolationsledeplade. 6. Separatorsystem, der omfatter: (a) separatorbeholder, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilken separatorbeholder er konstrueret ved sammenføjning afen flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) mindst én isolationsledeplade. 7. Proceskolonnesystem, der omfatter: (a) proceskolonne, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia) og ved en temperatur, der er lavere end ca. -40°0 (-40°F), hvilken proceskolonne er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) pakkemateriale. 8. Proceskolonnesystem, der omfatter: (a) proceskolonne, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilken proceskolonne er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) pakkemateriale. 9. Pumpesystem, der omfatter: (a) et pumpehus, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilket pumpehus er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (a) en drivkobling. 10. Pumpesystem, der omfatter: (a) et pumpehus, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilket pumpehus er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader haren tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) en drivkobling. 11. Afbrændingssystem, der omfatter: (a) en afbrændingssystemledning, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilken afbrændingssystemledning er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det undertryk stående fluid, og (b) en afbrændingssystem-scrubber. 12. Afbrændingssystem, der omfatter. (a) en afbrændingssystemledning, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilken afbrændingssystemledning er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) en afbrændingssystem-scrubber. 13. Strømningskanaldistributionsnetværkssystem, der omfatter: (a) mindst én opbevaringsbeholder, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilken opbevaringsbeholder, hvoraf der mindst er én, er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) mindst ét distributionsrør. 14. Strømningskanaldistributionsnetværkssystem, der omfatter: (a) mindst ét distributionsrør, der er velegnet til at indeholde et fluid ved et tryk, der er højere end ca. 1035 kPa (150 psia), og ved en temperatur, der er lavere end ca. -40°C (-40°F), hvilket distributionsrør, hvoraf der mindst er ét, er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde det under tryk stående fluid, og (b) mindst én opbevaringsbeholder. 15. Strømningskanaldistributionsnetværkssystem, der omfatter: (a) mindst én opbevaringsbeholder, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (-190°F) til ca. -62°C (-80°F), hvilken opbevaringsbeholder er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) mindst ét distributionsrør. 16. Strømningskanaldistributionsnetværkssystem, der omfatter: (a) mindst ét distributionsrør, der er velegnet til at indeholde under tryk stående fordråbet naturgas ved et tryk på fra ca. 1035 kPa (150 psia) til ca. 7590 kPa (1100 psia) og ved en temperatur på fra ca. -123°C (*190°F) til ca. -62°C (-80°F), hvilket distributionsrør er konstrueret ved sammenføjning af en flerhed af separate plader af materialer, der omfatter et lavlegeret stål med ultrahøj styrke indeholdende mindre end 9 vægtprocent nikkel og med en trækstyrke, der er større end 830 MPa (120 ksi), og en DBTT, der er lavere end ca. -73°C (-100°F), hvor sammenføjninger mellem de separate plader har en tilstrækkelig styrke og sejhed til under de pågældende tryk- og temperaturforhold at indeholde den under tryk stående fordråbede naturgas, og (b) mindst én opbevaringsbeholder.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US6820897P | 1997-12-19 | 1997-12-19 | |
US6820897 | 1997-12-19 | ||
PCT/US1998/012725 WO1999032837A1 (en) | 1997-12-19 | 1998-06-18 | Process components, containers, and pipes suitable for containing and transporting cryogenic temperature fluids |
US9812725 | 1998-06-18 |
Publications (2)
Publication Number | Publication Date |
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DK200000939A true DK200000939A (da) | 2000-06-16 |
DK174826B1 DK174826B1 (da) | 2003-12-08 |
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ID=22081107
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK200000939A DK174826B1 (da) | 1997-12-19 | 2000-06-16 | Proceskomponenter, beholdere og rør, der er velegnede til at indeholde og transportere fluider ved kryogene temperaturer |
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Families Citing this family (57)
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EP1801254A1 (de) * | 2005-12-20 | 2007-06-27 | Siemens Aktiengesellschaft | Verdichtergehäuse aus Gussstahl für Tieftemperaturanwendungen |
EP1832667A1 (fr) | 2006-03-07 | 2007-09-12 | ARCELOR France | Procédé de fabrication de tôles d'acier à très hautes caractéristiques de résistance, de ductilité et de tenacité, et tôles ainsi produites |
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