US20080127675A1 - Cold Box and Cryogenic Plant Including a Cold Box - Google Patents
Cold Box and Cryogenic Plant Including a Cold Box Download PDFInfo
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- US20080127675A1 US20080127675A1 US12/029,563 US2956308A US2008127675A1 US 20080127675 A1 US20080127675 A1 US 20080127675A1 US 2956308 A US2956308 A US 2956308A US 2008127675 A1 US2008127675 A1 US 2008127675A1
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- cryogenic
- housing
- cold box
- wall
- columns
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Classifications
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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
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/001—Thermal insulation specially adapted for cryogenic vessels
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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
- 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
- F25J3/04406—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 a dual pressure main column system
- F25J3/04412—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 a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
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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
- 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.
- F25J3/04878—Side by side arrangement of multiple vessels in a main column system, wherein the vessels are normally mounted one upon the other or forming different sections of the same column
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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
- 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"
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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
- 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
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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
- 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
- F25J3/04975—Construction and layout of air fractionation equipments, e.g. valves, machines adapted for special use of the air fractionation unit, e.g. transportable devices by truck or small scale use
- F25J3/04987—Construction and layout of air fractionation equipments, e.g. valves, machines adapted for special use of the air fractionation unit, e.g. transportable devices by truck or small scale use for offshore use
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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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0104—Shape cylindrical
- F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
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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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/03—Orientation
- F17C2201/032—Orientation with substantially vertical main axis
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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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/05—Size
- F17C2201/054—Size medium (>1 m3)
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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
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0337—Granular
- F17C2203/0341—Perlite
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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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/01—Mounting arrangements
- F17C2205/0103—Exterior arrangements
- F17C2205/0111—Boxes
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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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/011—Oxygen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
- F17C2223/033—Small pressure, e.g. for liquefied gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0135—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
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
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- 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
- Y10S62/907—Insulation
Definitions
- the present invention relates to a cold box and a cryogenic plant including a cold box. It applies in particular to cold boxes containing cryogenic liquefiers and/or cryogenic distillation plants and especially applies to cold boxes located on ships.
- the cryogenic distillation plant may be an air separation unit for production of oxygen and/or nitrogen for off shore applications such as drilling platforms.
- U.S. Pat. No. 6,101,840 describes a cold box having a protuberance containing part of an air separation unit. It is not possible to gain access to the contents of the protuberance without damaging the cold box.
- U.S. Pat. No. 6,360,545 describes a cold box for shipboard use, wherein the cold box contains an air separation unit.
- U.S. Pat. No. 6,378,331 describes a cold box for shipboard use wherein the cold box contains columns and main heat exchanger of an air separation unit.
- the cold box includes a double walled structure containing perlite between the walls and the elements of the air separation unit are housed within the inner wall of the structure without any perlite around them.
- a cold box which will allow for improved access to facilitate maintenance of elements within a cold box comprising:
- thermal insulator filling at least part of the space between the inner and outer walls of the outer jacket.
- Other optional features may include one or more of the following:
- the base and inner wall of the outer jacket are impermeable to liquid.
- the cold box may be applied to cryogenic plant, an air distillation plant, or to a ship.
- the main cryogenic elements are elements, which normally function at temperatures below ⁇ 50° C.
- the auxiliary element within the housing may also function at a temperature of below ⁇ 50° C.
- FIG. 1 is an illustration of one embodiment of the invention.
- FIG. 2 is an illustration of a second embodiment.
- a cold box which will allow for improved access to facilitate maintenance of elements within a cold box comprising:
- thermal insulator filling at least part of the space between the inner and outer walls of the outer jacket.
- Other optional features may include one or more of the following:
- the cold box may be applied to cryogenic plant, an air distillation plant, or to a ship.
- the main cryogenic elements are elements, which normally function at temperatures below ⁇ 50° C.
- the auxiliary element within the housing may also function at a temperature of below ⁇ 50° C.
- FIG. 1 illustrates a cut away view of an air distillation plant according to one embodiment of the invention.
- the invention and its corresponding embodiments, is described below in relation to cold boxes containing an air separation unit, but also applies to cold boxes containing additionally, or alternatively, at least one storage tank for cryogenic liquids.
- the air distillation plant comprises a main cryogenic element, such as a high-pressure column 1 and a low-pressure column 3 , which are thermally integrated.
- the two columns are placed within an outer jacket 7 having a circular cross section.
- the outer jacket 7 also referred to herein as the cold box, is made of resilient metal, such as stainless steel or aluminum, is placed on top of a metal framework, sometimes known as a “pancake”, which is fastened to the deck 27 of a ship or floating platform.
- Cooled compressed air to be sent to the high-pressure column is sent to a heat exchanger (not shown) outside the cold box via piping duct 9 .
- the piping duct also carries conduits containing product and waste steams from the columns.
- One of the products is a pressurised liquid oxygen stream, which is to be vaporised in the heat exchange line.
- the liquid oxygen is removed from the low-pressure column, pressurised by an auxiliary element 16 , such as a pump, and sent to the piping duct 9 in a conduit.
- the pump is located in a housing 13 , which extends through an opening in the outer jacket such that the housing is directly accessible from outside the outer jacket 7 .
- the housing 13 is made of resilient metal, such as stainless steel or aluminium.
- the space between the cold box and the columns is filled at least partially with particulate insulation material, such as perlite.
- the cold box illustrated has a circular cross-section, but any cross-section could be used.
- the low-pressure column 3 is placed on a structure 11 so as to prevent cold migration to the ship or platform deck 27 , which could cause the carbon steel structure of the ship to fracture.
- the high-pressure column 1 is similarly insulated from the deck.
- the housing 13 is sealed into an opening in the outer jacket 7 , preferably welded to the inner wall 31 , such that the perlite cannot escape.
- the housing is insulated from the interior of the cold box using a rock wool layer 15 and a non-resilient metal wall 17 , such as an expanded metal layer. These layers form a weak link, which will break in the case of over-pressure allowing the liquid oxygen to flow back into the cold box 7 .
- the housing 13 is in the form of a cuboid that has an inner space 14 and a base wall 29 which slopes downwards towards the deck 27 of the ship, to assist the flow of any leaking liquid oxygen back into the cold box 7 after breaking through the metal wall 17 .
- the housing may have any suitable shape.
- the base 12 of the cold box is insulated using a layer of foam glass 19 covered by a sealing plate 21 .
- the bottom of both column structures 11 is partially filled with a layer of rock wool 23 .
- the cold box may also be opened via an access door 25 .
- the housing 13 is insulated using perlite or rock wool and as well as (or instead of) a pump or pumps and their associated piping may contain at least one turboexpander and/or at least one valve and/or other piping.
- the outer jacket 7 has an inner wall 31 and an outer wall 33 , at least part of the space between the two being filled with perlite 35 in loose form or in the form of bricks. If the insulant is in the form of bricks, the inner wall of the jacket may be formed by the sidewalls of the bricks or may be a separate panel.
- the sealing plate 21 and inner walls 31 of the outer jacket are impervious to liquid, so that if any cryogenic liquid escapes from the air separation unit will collect in the bottom of the cold box and eventually evaporates or is vaporised using a vaporiser.
- a relief valve may be provided so that vapors leaking from the cryogenic unit may escape from the outer jacket.
- the air separation unit may have any number of columns.
- it may comprise a single column, a double column, or a triple column.
- a mixing column or an argon production column may be used.
- the invention has been described in relation to cold boxes containing an air separation unit, but also applies to cold boxes containing additionally or alternatively, at least one storage tank for cryogenic liquids. It also applies to cold boxes containing a liquefier for producing cryogenic liquids.
- the air separation unit could be replaced by any cryogenic distillation unit, such as a unit for separating a mixture having principal components in the group comprising hydrogen, helium, methane, nitrogen, and carbon monoxide.
- cryogenic distillation unit such as a unit for separating a mixture having principal components in the group comprising hydrogen, helium, methane, nitrogen, and carbon monoxide.
- the methods to make such a replacement are well known to those skilled in the art.
- the invention also relates to cold boxes in which cryogenic liquids other than oxygen is pumped, such as nitrogen.
- cryogenic liquids other than oxygen is pumped, such as nitrogen.
- the skill to do such an application is well known to those skilled in the art.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
This disclosure discusses providing safer and more accessible insulating cold boxes for cryogenic equipment. A cold box of the current invention includes a housing partially extending out of the cold box jacket wherein equipment that may need to be accessed can be located. The housing includes a breakaway barrier between the main cold box and the external housing to allow overpressures to be relieved into the cold box. Cold boxes may contain cryogenic columns, sections of cryogenic columns, distillation columns, mixing columns, storage vessels, pressure vessels, heat exchangers, and combinations thereof. The housing may contain auxiliary elements such as rotating equipment, pumps, turboexpanders, instrument devices, valves, and piping. Placing auxiliary elements in a housing outside the main cold box allows for safer access to cryogenic equipment.
Description
- The present invention relates to a cold box and a cryogenic plant including a cold box. It applies in particular to cold boxes containing cryogenic liquefiers and/or cryogenic distillation plants and especially applies to cold boxes located on ships. The cryogenic distillation plant may be an air separation unit for production of oxygen and/or nitrogen for off shore applications such as drilling platforms.
- U.S. Pat. No. 6,101,840 describes a cold box having a protuberance containing part of an air separation unit. It is not possible to gain access to the contents of the protuberance without damaging the cold box.
- U.S. Pat. No. 6,360,545 describes a cold box for shipboard use, wherein the cold box contains an air separation unit.
- U.S. Pat. No. 6,378,331 describes a cold box for shipboard use wherein the cold box contains columns and main heat exchanger of an air separation unit. The cold box includes a double walled structure containing perlite between the walls and the elements of the air separation unit are housed within the inner wall of the structure without any perlite around them.
- “Tonnage Nitrogen Generation for Oil and Gas Enhanced recovery in the North Sea” by Goldstone and Ralston presented in the Annual Report, Session 6 of the 9th Continental Meeting of Gas Processors Association, 1992 describes an air separation unit for use on an oil platform.
- It is an objective of the invention to provide a cold box with improved safety in particular for off shore applications, such as Fischer Tropsch conversion.
- It is another objective of the invention to facilitate maintenance of elements of the cold box.
- According to the invention, there is provided a cold box, which will allow for improved access to facilitate maintenance of elements within a cold box comprising:
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- (a) a cryogenic assembly comprising the main cryogenic elements and additional auxiliary elements, wherein each main cryogenic element is selected from the group consisting of cryogenic columns, sections of such columns, storage vessels, heat exchangers and superposed combinations thereof;
- (b) an outer jacket surrounding at least some of the main cryogenic elements of the cryogenic assembly, wherein the outer jacket has an outer wall and an inner wall, and
- (c) a base; and
- (d) a housing, wherein the housing contains at least one of the auxiliary elements and the auxiliary element extends at least partially outside the outer jacket, and that particular auxiliary element is connected to at least one of the main cryogenic elements within the outer jacket.
- Typically, there is at least one thermal insulator filling at least part of the space between the inner and outer walls of the outer jacket. Other optional features may include one or more of the following:
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- the auxiliary element is selected from the group comprising pumps, turboexpanders, valves and piping;
- each main cryogenic element is selected from the group consisting of distillation columns, mixing columns, storage vessels, heat exchangers and superposed combinations thereof;
- there is free space between the cryogenic assembly and the inner wall of the outer jacket;
- the housing is attached to the inner wall of the outer jacket;
- at least one thermal insulator is perlite;
- the housing is made a material chosen from the group comprising steel and aluminium;
- the auxiliary element is insulated from the cryogenic assembly within the outer jacket by a barrier;
- the barrier forms a weak seal, such as in the case of over pressure within the housing, the insulation barrier breaks;
- the barrier is made of material chosen from the group comprising perlite, vermiculite, rock wool and metal;
- the housing is situated from about 1 to from about 5 meters above the base;
- the base and inner walls are impermeable to liquid leaking from the cryogenic assembly;
- the housing extends within the space between the inner and outer walls of the outer jacket; and
- the base and inner wall of the outer jacket are impermeable to liquid.
- According to additional embodiments of the invention, the cold box may be applied to cryogenic plant, an air distillation plant, or to a ship.
- The main cryogenic elements are elements, which normally function at temperatures below −50° C.
- The auxiliary element within the housing may also function at a temperature of below −50° C.
- For a further understanding of the nature and objects for the present invention, reference should be made to the following detailed description, taken in conjunction with the accompanying drawings, in which like elements are given the same or analogous reference numbers and wherein:
-
FIG. 1 is an illustration of one embodiment of the invention; and -
FIG. 2 is an illustration of a second embodiment. - According to the invention, there is provided a cold box, which will allow for improved access to facilitate maintenance of elements within a cold box comprising:
-
- (a) a cryogenic assembly comprising the main cryogenic elements and additional auxiliary elements, wherein each main cryogenic element is selected from the group consisting of cryogenic columns, sections of such columns, storage vessels, heat exchangers and superposed combinations thereof;
- (b) an outer jacket surrounding at least some of the main cryogenic elements of the cryogenic assembly, wherein the outer jacket has an outer wall and an inner wall, and
- (c) a base; and
- (d) a housing, wherein the housing contains at least one of the auxiliary elements and the auxiliary element extends at least partially outside the outer jacket, and that particular auxiliary element is connected to at least one of the main cryogenic elements within the outer jacket.
- Typically, there is at least one thermal insulator filling at least part of the space between the inner and outer walls of the outer jacket. Other optional features may include one or more of the following:
-
- the auxiliary element is selected from the group comprising pumps, turboexpanders, valves and piping;
- each main cryogenic element is selected from the group consisting of distillation columns, mixing columns, storage vessels, heat exchangers and superposed combinations thereof;
- there is free space between the cryogenic assembly and the inner wall of the outer jacket;
- the housing is attached to the inner wall of the outer jacket;
- at least one thermal insulator is perlite;
- the housing is made a material chosen from the group comprising steel and aluminium;
- the auxiliary element is insulated from the cryogenic assembly within the outer jacket by a barrier;
- the barrier forms a weak seal, such as in the case of over pressure within the housing, the insulation barrier breaks;
- the barrier is made of material chosen from the group comprising perlite, vermiculite, rock wool and metal;
- the housing is situated from about 1 to from about 5 meters above the base;
- the base and inner walls are impermeable to liquid leaking from the cryogenic assembly;
- the housing extends within the space between the inner and outer walls of the outer jacket; and
- the base and inner wall of the outer jacket are impermeable to liquid.
- According to additional embodiments of the invention, the cold box may be applied to cryogenic plant, an air distillation plant, or to a ship.
- The main cryogenic elements are elements, which normally function at temperatures below −50° C.
- The auxiliary element within the housing may also function at a temperature of below −50° C.
-
FIG. 1 illustrates a cut away view of an air distillation plant according to one embodiment of the invention. The invention and its corresponding embodiments, is described below in relation to cold boxes containing an air separation unit, but also applies to cold boxes containing additionally, or alternatively, at least one storage tank for cryogenic liquids. - The air distillation plant comprises a main cryogenic element, such as a high-pressure column 1 and a low-
pressure column 3, which are thermally integrated. The two columns are placed within an outer jacket 7 having a circular cross section. The outer jacket 7, also referred to herein as the cold box, is made of resilient metal, such as stainless steel or aluminum, is placed on top of a metal framework, sometimes known as a “pancake”, which is fastened to thedeck 27 of a ship or floating platform. - Cooled compressed air to be sent to the high-pressure column is sent to a heat exchanger (not shown) outside the cold box via piping duct 9. The piping duct also carries conduits containing product and waste steams from the columns. One of the products is a pressurised liquid oxygen stream, which is to be vaporised in the heat exchange line. The liquid oxygen is removed from the low-pressure column, pressurised by an auxiliary element 16, such as a pump, and sent to the piping duct 9 in a conduit. The pump is located in a
housing 13, which extends through an opening in the outer jacket such that the housing is directly accessible from outside the outer jacket 7. Thehousing 13 is made of resilient metal, such as stainless steel or aluminium. The space between the cold box and the columns is filled at least partially with particulate insulation material, such as perlite. - The cold box illustrated has a circular cross-section, but any cross-section could be used.
- The low-
pressure column 3 is placed on a structure 11 so as to prevent cold migration to the ship orplatform deck 27, which could cause the carbon steel structure of the ship to fracture. The high-pressure column 1 is similarly insulated from the deck. - As shown in
FIG. 2 , thehousing 13 is sealed into an opening in the outer jacket 7, preferably welded to the inner wall 31, such that the perlite cannot escape. The housing is insulated from the interior of the cold box using arock wool layer 15 and a non-resilient metal wall 17, such as an expanded metal layer. These layers form a weak link, which will break in the case of over-pressure allowing the liquid oxygen to flow back into the cold box 7. - The
housing 13 is in the form of a cuboid that has an inner space 14 and a base wall 29 which slopes downwards towards thedeck 27 of the ship, to assist the flow of any leaking liquid oxygen back into the cold box 7 after breaking through the metal wall 17. The housing may have any suitable shape. - The
base 12 of the cold box is insulated using a layer of foam glass 19 covered by a sealing plate 21. The bottom of both column structures 11 is partially filled with a layer ofrock wool 23. - The cold box may also be opened via an
access door 25. - The
housing 13 is insulated using perlite or rock wool and as well as (or instead of) a pump or pumps and their associated piping may contain at least one turboexpander and/or at least one valve and/or other piping. - The outer jacket 7 has an inner wall 31 and an outer wall 33, at least part of the space between the two being filled with perlite 35 in loose form or in the form of bricks. If the insulant is in the form of bricks, the inner wall of the jacket may be formed by the sidewalls of the bricks or may be a separate panel.
- The sealing plate 21 and inner walls 31 of the outer jacket are impervious to liquid, so that if any cryogenic liquid escapes from the air separation unit will collect in the bottom of the cold box and eventually evaporates or is vaporised using a vaporiser.
- A relief valve may be provided so that vapors leaking from the cryogenic unit may escape from the outer jacket.
- One skilled in the art will appreciate that the air separation unit may have any number of columns. For example, it may comprise a single column, a double column, or a triple column. Additionally, a mixing column or an argon production column may be used.
- The invention has been described in relation to cold boxes containing an air separation unit, but also applies to cold boxes containing additionally or alternatively, at least one storage tank for cryogenic liquids. It also applies to cold boxes containing a liquefier for producing cryogenic liquids.
- Similarly, the air separation unit could be replaced by any cryogenic distillation unit, such as a unit for separating a mixture having principal components in the group comprising hydrogen, helium, methane, nitrogen, and carbon monoxide. The methods to make such a replacement are well known to those skilled in the art.
- The invention also relates to cold boxes in which cryogenic liquids other than oxygen is pumped, such as nitrogen. The skill to do such an application is well known to those skilled in the art.
- Preferred processes and apparatus for practicing the present invention have been described. It will be understood and readily apparent to the skilled artisan that many changes and modifications may be made to the above-described embodiments without departing from the spirit and the scope of the present invention. The foregoing is illustrative only and that other embodiments of the integrated processes and apparatus may be employed without departing from the true scope of the invention defined in the following claims.
Claims (16)
1-20. (canceled)
21. A cold box apparatus comprising:
(a) a cryogenic assembly comprising:
(1) a main cryogenic element, and
(2) an auxiliary element having a first part and a second part,
wherein said first part is connected to said main cryogenic element,
(b) an outer jacket comprising:
(1) an outer wall,
(2) an inner wall, and
(3) a first space between said inner wall and said outer wall,
wherein said outer jacket surrounds at least some of said main cryogenic element, and wherein there is a second space between said outer jacket and said main cryogenic element,
(c) a base, and
(d) a housing comprising an inner space, wherein said housing extends at least partially outside said outer jacket, and wherein said second part of said auxiliary element extends at least partially into said inner space of said housing.
22. The apparatus of claim 21 , wherein said auxiliary element is selected from the group consisting of rotating equipment, pumps, turboexpanders, instrument devices, valves, and piping.
23. The apparatus of claim 21 , wherein said main cryogenic element is selected from the group consisting of cryogenic columns, sections of cryogenic columns, distillation columns, mixing columns, storage vessels, pressure vessels, heat exchangers, and combinations thereof.
24. The apparatus of claim 21 , wherein said second space is at least partially filled with insulating material.
25. The apparatus of claim 21 , wherein said housing is attached to the inner wall of said outer jacket.
26. The apparatus of claim 21 , further comprising a thermal insulator filling at least part of said first space.
27. The apparatus of claim 26 , wherein said thermal insulator comprises perlite.
28. The apparatus of claim 21 , wherein said housing is made of a material selected from the group consisting of steel, stainless steel, aluminum, and alloys thereof.
29. The apparatus of claim 21 , wherein said auxiliary element is insulated from said main cryogenic element by a barrier.
30. The apparatus of claim 28 , wherein said barrier is made of material selected from the group consisting of perlite, vermiculite, rock wool, and metal.
31. The apparatus of claim 21 , wherein said base and said inner wall are impermeable to liquid leaking from said cryogenic assembly.
32. The apparatus of claim 21 , further comprising a sealing plate, wherein said sealing plate and said inner wall are impermeable to liquid.
33. The apparatus of claim 21 , wherein said apparatus is bolted to the deck of a ship.
34. A cryogenic plant comprising the apparatus of claim 21 .
35. An air distillation plant apparatus comprising the apparatus of claim 32 .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/029,563 US20080127675A1 (en) | 2004-10-25 | 2008-02-12 | Cold Box and Cryogenic Plant Including a Cold Box |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/972,828 US7340921B2 (en) | 2004-10-25 | 2004-10-25 | Cold box and cryogenic plant including a cold box |
US12/029,563 US20080127675A1 (en) | 2004-10-25 | 2008-02-12 | Cold Box and Cryogenic Plant Including a Cold Box |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US10/972,828 Continuation US7340921B2 (en) | 2004-10-25 | 2004-10-25 | Cold box and cryogenic plant including a cold box |
Publications (1)
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US20080127675A1 true US20080127675A1 (en) | 2008-06-05 |
Family
ID=35285612
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
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US10/972,828 Expired - Fee Related US7340921B2 (en) | 2004-10-25 | 2004-10-25 | Cold box and cryogenic plant including a cold box |
US12/029,563 Abandoned US20080127675A1 (en) | 2004-10-25 | 2008-02-12 | Cold Box and Cryogenic Plant Including a Cold Box |
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US10/972,828 Expired - Fee Related US7340921B2 (en) | 2004-10-25 | 2004-10-25 | Cold box and cryogenic plant including a cold box |
Country Status (6)
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US (2) | US7340921B2 (en) |
EP (1) | EP1807670A1 (en) |
AU (1) | AU2005298740B2 (en) |
MX (1) | MX2007004724A (en) |
NO (1) | NO20071770L (en) |
WO (1) | WO2006045675A1 (en) |
Cited By (1)
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US20100139208A1 (en) * | 2008-12-10 | 2010-06-10 | Air Liquide Process And Construction Inc. | Hybrid Method Of Erecting A Cold Box Using Prefabricated And Field Erected Components |
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US7340921B2 (en) * | 2004-10-25 | 2008-03-11 | L'Air Liquide - Société Anonyme à Directoire et Conseil de Surveillance pour l'Etude et l'Exploitation des Procédés Georges Claude | Cold box and cryogenic plant including a cold box |
US9086235B2 (en) | 2006-11-30 | 2015-07-21 | Praxair Technology, Inc. | Insulation arrangement |
CN101858684B (en) * | 2010-07-13 | 2012-03-07 | 中国化学工程第四建设有限公司 | Air separation cooling box layering haling method |
US8727159B2 (en) * | 2011-04-12 | 2014-05-20 | Conocophillips Company | Cold box design providing secondary containment |
FR2995673B1 (en) * | 2012-09-19 | 2018-08-10 | L'air Liquide,Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | HEAT EXCHANGER AND EXCHANGER ASSEMBLY FOR AIR DISTILLATION COMPRISING SUCH HEAT EXCHANGERS |
US20140087102A1 (en) * | 2012-09-21 | 2014-03-27 | Air Liquide Large Industries U.S. Lp | Air separation column low-density solid-state insulation patent |
US10145514B2 (en) | 2013-11-18 | 2018-12-04 | Man Energy Solutions Se | Cold-box system and method for power management aboard ships |
FR3017938B1 (en) * | 2014-02-24 | 2019-03-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | CRYOGENIC DISTILLATION AIR SEPARATION APPARATUS WITH SAFELY PLATFORM |
WO2015124853A2 (en) | 2014-02-24 | 2015-08-27 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Apparatus for air separation by cryogenic distillation, having an elevated platform |
FR3017939B1 (en) * | 2014-02-24 | 2019-03-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | CRYOGENIC DISTILLATION SEPARATION APPARATUS COMPRISING A PLURALITY OF MODULAR ELEMENTS |
RU169852U1 (en) * | 2016-05-24 | 2017-04-04 | Публичное акционерное общество криогенного машиностроения (ПАО "Криогенмаш") | Cryogenic installation casing |
CN110268215B (en) * | 2017-01-10 | 2021-09-03 | 乔治洛德方法研究和开发液化空气有限公司 | Enclosure for an apparatus for separating a gaseous mixture by distillation and separation apparatus comprising such an enclosure |
CN109954367A (en) * | 2017-12-14 | 2019-07-02 | 乔治洛德方法研究和开发液化空气有限公司 | It is separated by distillation the sealing cover of the equipment of gaseous mixture and the equipment including sealing cover |
FR3095217B1 (en) * | 2019-04-17 | 2021-03-19 | Air Liquide | Frame panel intended to be part of a cold box of a separation device |
CN110553153B (en) * | 2019-09-26 | 2020-09-29 | 宝武集团鄂城钢铁有限公司 | Method for treating leakage of liquid nitrogen, liquid argon or liquid air in cold box by local sand raking |
US11415256B2 (en) * | 2019-12-12 | 2022-08-16 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Apparatus for the separation or liquefaction of a gas operating at cryogenic temperatures |
FR3123113B1 (en) * | 2021-05-19 | 2023-06-09 | Air Liquide | Distillation column and method of transporting a distillation column |
CN113958801B (en) * | 2021-10-09 | 2023-02-17 | 中国化学工程第六建设有限公司 | Column base bottom plate separated large-scale integral cold box and installation method thereof |
FR3138325A1 (en) * | 2022-07-29 | 2024-02-02 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Column enclosure for distillation at low temperatures |
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Also Published As
Publication number | Publication date |
---|---|
EP1807670A1 (en) | 2007-07-18 |
US7340921B2 (en) | 2008-03-11 |
NO20071770L (en) | 2007-07-25 |
AU2005298740B2 (en) | 2010-02-18 |
AU2005298740A1 (en) | 2006-05-04 |
WO2006045675A1 (en) | 2006-05-04 |
MX2007004724A (en) | 2007-06-15 |
US20060086141A1 (en) | 2006-04-27 |
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