FR2917490A1 - Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure - Google Patents
Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure Download PDFInfo
- Publication number
- FR2917490A1 FR2917490A1 FR0755699A FR0755699A FR2917490A1 FR 2917490 A1 FR2917490 A1 FR 2917490A1 FR 0755699 A FR0755699 A FR 0755699A FR 0755699 A FR0755699 A FR 0755699A FR 2917490 A1 FR2917490 A1 FR 2917490A1
- Authority
- FR
- France
- Prior art keywords
- enclosure
- separated
- cold box
- air
- box according
- 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.)
- Withdrawn
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 20
- 238000004821 distillation Methods 0.000 title claims abstract description 12
- 230000006835 compression Effects 0.000 title claims abstract description 6
- 238000007906 compression Methods 0.000 title claims abstract description 6
- 238000000926 separation method Methods 0.000 title claims description 13
- 238000004140 cleaning Methods 0.000 title abstract description 3
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims 1
- 230000005540 biological transmission Effects 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- 239000002912 waste gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 239000002699 waste material Substances 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
- F25J3/044—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 single pressure main column system only
-
- 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
- F25J3/0204—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 characterised by the feed stream
- F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- 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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0252—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 characterised by the separated product stream separation of hydrogen
-
- 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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0261—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 characterised by the separated product stream separation of carbon monoxide
-
- 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
- F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
- F25J3/04254—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using the cold stored in external cryogenic fluids
-
- 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/42—Nitrogen
-
- 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
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/40—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being air
-
- 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
- F25J2280/00—Control of the process or apparatus
- F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
-
- 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
-
- 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
- F25J2290/62—Details of storing a fluid in a tank
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
La présente invention est relative à une boîte froide d'un appareil deThe present invention relates to a cold box of an apparatus for
séparation cryogénique par distillation. En général quand un appareil de séparation cryogénique est construit sur site, il faut installer un compresseur, un appareil d'épuration, une boîte froide, un stockage de liquide et un système de vaporisation. Chaque élément est généralement installé séparément et donc doit être connecté à au moins un autre élément sur site, ce qui peut être coûteux en temps et en main d'oeuvre. Selon la présente invention, il est prévu une boîte froide d'un appareil de séparation cryogénique par distillation comprenant i) une enceinte isolée ii) une colonne de distillation contenue à l'intérieur de l'enceinte iii) des moyens pour envoyer un fluide à séparer à la colonne iv) des moyens pour sortir un fluide séparé de la colonne caractérisée en ce qu'au moins un élément de traitement d'un fluide, soit séparé dans la colonne soit à séparer dans la colonne, est monté sur une paroi extérieure de l'enceinte. Selon d'autres aspects facultatifs : - au moins un stockage de liquide cryogénique est à l'intérieur de l'enceinte. - au moins un élément de traitement d'un fluide monté sur une paroi extérieure de l'enceinte est un élément de traitement de fluide séparé. - au moins un élément est une vanne, un échangeur, un compresseur, une pompe, un instrument de mesure ou d'analyse. - au moins un élément de traitement d'un fluide monté sur une paroi extérieure de l'enceinte est un élément de traitement de fluide à séparer. - au moins un élément fait partie de ou constitue une unité d'épuration. - au moins un élément fait partie de ou constitue une unité de compression. au moins un élément est, de préférence entièrement, supporté par l'enceinte. - l'au moins un élément est monté sur une paroi latérale de l'enceinte. Selon un autre aspect de l'invention, il est prévu un appareil de séparation cryogénique comprenant une boîte froide telle que décrite ci-dessus. cryogenic separation by distillation. In general, when a cryogenic separation apparatus is built on site, a compressor, a purifier, a cold box, a liquid storage and a vaporization system must be installed. Each element is usually installed separately and therefore must be connected to at least one other element on site, which can be costly in time and manpower. According to the present invention, there is provided a cold box of a cryogenic separation apparatus by distillation comprising i) an isolated chamber ii) a distillation column contained inside the enclosure iii) means for sending a fluid to separating in column iv) means for removing a fluid separated from the column characterized in that at least one fluid treatment element, is separated in the column or to be separated in the column, is mounted on an outer wall of the enclosure. According to other optional aspects: at least one storage of cryogenic liquid is inside the enclosure. at least one fluid treatment element mounted on an outer wall of the enclosure is a separate fluid treatment element. at least one element is a valve, an exchanger, a compressor, a pump, a measurement or analysis instrument. - At least one fluid treatment element mounted on an outer wall of the enclosure is a fluid treatment element to be separated. - at least one element is part of or constitutes a purification unit. at least one element is part of or constitutes a compression unit. at least one element is preferably entirely supported by the enclosure. - The at least one element is mounted on a side wall of the enclosure. According to another aspect of the invention, there is provided a cryogenic separation apparatus comprising a cold box as described above.
L'appareil peut être un appareil de séparation d'air . L'invention sera décrite en plus de détail en se référant à la figure qui illustre un appareil de séparation d'air pour la production d'azote selon l'invention. The apparatus may be an air separation apparatus. The invention will be described in more detail with reference to the figure which illustrates an air separation apparatus for the production of nitrogen according to the invention.
L'appareil est dans ce cas précis tenu en froid, non pas par une turbine, mais par injection d'azote liquide en tête de colonne, de manière connue, appelée communément biberonnage . L'appareil comprend une boîte froide 1 constituée par une enceinte allongée 9 d'axe vertical dans laquelle se trouvent une colonne de distillation d'air 5 munie d'un condenseur de tête, une ligne d'échange 6, servant à refroidir de l'air comprimé et épuré par échange de chaleur avec de l'azote et un gaz résiduaire, et un stockage d'azote liquide 7. La boîte froide est isolée en étant perlitée et mise sous vide. Alternativement elle peut contenir de la perlite seule ou un autre isolant. L'enceinte 9 peut être à section circulaire ou rectangulaire. In this case, the apparatus is in fact kept cold, not by a turbine, but by injecting liquid nitrogen at the top of the column, in a known manner, commonly known as biberonnage. The apparatus comprises a cold box 1 constituted by an elongated enclosure 9 of vertical axis in which there is an air distillation column 5 provided with a head condenser, an exchange line 6, for cooling the compressed and purified air by heat exchange with nitrogen and a waste gas, and storage of liquid nitrogen 7. The cold box is isolated by being pearled and placed under vacuum. Alternatively it may contain perlite alone or another insulator. The enclosure 9 may be circular or rectangular section.
La boîte froide est posée sur le sol 3 et maintenue en place par une jupe 17 (ou par des pieds). Divers éléments 11, 13, 15 de l'appareil de séparation cryogénique sont fixés à la paroi latérale extérieure de la boîte froide. Ces éléments peuvent traiter au moins une partie de l'air à séparer ou au moins une partie de l'azote séparé ou du résiduaire. Par exemple, l'unité d'épuration d'air 11 comprenant les bouteilles d'adsorbant, le réchauffeur électrique et les vannes et tuyaux associés peut être fixée à la paroi extérieure de l'enceinte 9. L'unité d'épuration est connectée lors de la fixation à la colonne pour permettre le passage d'air épuré à la colonne à travers la conduite 19 et de gaz résiduaire de la colonne à l'épuration pour la régénération (non-illustré). Une unité de traitement 13 d'un produit de la distillation dans la colonne de l'appareil est également fixée à la paroi extérieure. Elle peut comprendre une unité d'analyse et/ou une unité de mesure (tel qu'un débitmètre) et/ou une vanne de détente et/ou une pompe et/ou un échangeur et/ou une turbine et/ou un compresseur d'azote et/ou un tuyau, en particulier de mise à l'air. L'unité de traitement est connectée par une conduite d'azote 21 ou de gaz résiduaire (non-illustré) à la colonne, lors de la fixation. The cold box is placed on the floor 3 and held in place by a skirt 17 (or feet). Various elements 11, 13, 15 of the cryogenic separation apparatus are attached to the outer side wall of the cold box. These elements can treat at least a portion of the air to be separated or at least a portion of the separated nitrogen or waste. For example, the air cleaning unit 11 comprising the adsorbent bottles, the electric heater and the associated valves and pipes can be attached to the outer wall of the enclosure 9. The purification unit is connected when attached to the column to allow the passage of purified air to the column through the pipe 19 and waste gas from the column to the purification for regeneration (not shown). A treatment unit 13 of a distillation product in the column of the apparatus is also attached to the outer wall. It may comprise an analysis unit and / or a measuring unit (such as a flow meter) and / or an expansion valve and / or a pump and / or exchanger and / or a turbine and / or a compressor. nitrogen and / or a pipe, in particular venting. The processing unit is connected by a nitrogen pipe 21 or waste gas (not shown) to the column, during attachment.
L'unité de compression d'air 15 peut être fixée à la paroi extérieure de l'enceinte ou être posée sur le sol sans être attaché à l'enceinte. Au moment où l'unité de compression d'air 15 est fixée à l'enceinte, elle est également rattachée à l'unité d'épuration 11 pour permettre le passage d'air comprimé de l'unité 15 à l'unité 11. On comprendra que comme la ou les connexion(s) entre la colonne et au moins une unité fixée à l'enceinte est (sont) effectuée(s) au moment où l'unité est fixée à l'enceinte, ces connexions n'ont plus besoin d'être effectuées sur site, ainsi simplifiant l'installation. The air compression unit 15 may be attached to the outer wall of the enclosure or placed on the floor without being attached to the enclosure. At the moment when the air compression unit 15 is attached to the enclosure, it is also attached to the purification unit 11 to allow the passage of compressed air from the unit 15 to the unit 11. It will be understood that since the connection (s) between the column and at least one unit attached to the enclosure is (are) performed at the moment the unit is attached to the enclosure, these connections have not been made. no need to be done on site, thus simplifying the installation.
Cette méthode de fixation des éléments peut également simplifier la mise en conteneur de l'appareil pour le transport de celui-ci. Par contre, un ou plusieurs éléments, destiné à être attaché à l'enceinte 9 quand la boîte froide fonctionne, peut être transporté sans être attaché à l'enceinte, la fixation à l'enceinte étant effectuée une fois arrivé sur site. This method of fixing the elements can also simplify the containerization of the apparatus for the transport thereof. On the other hand, one or more elements, intended to be attached to the enclosure 9 when the cold box is operating, can be transported without being attached to the enclosure, the fixing to the enclosure being carried out once on site.
L'invention s'applique à d'autres types de distillation que la séparation d'air, par exemple, les séparations de mélanges riches en hydrogène ou monoxyde de carbone et les mélanges riches en dioxyde de carbone. Il sera compris que l'invention peut s'appliquer à des appareils tenus en froid autrement que par biberonnage et que, même pour un appareil biberonné, le stockage de liquide n'est pas nécessairement à l'intérieur de l'enceinte. Le positionnement des unités montré sur la figure n'est qu'un exemple et les unités peuvent être disposées autrement. De même, la disposition spatiale des éléments à l'intérieur de l'enceinte ne représente pas forcément la réalité physique. Par exemple, la ligne d'échange peut être à côté de la colonne ou au-dessus de la colonne. En particulier, au moins un élément de traitement d'un fluide monté sur une paroi extérieure de l'enceinte est un élément de traitement de fluide séparé autre qu'un échangeur. The invention is applicable to other types of distillation than air separation, for example separations of mixtures rich in hydrogen or carbon monoxide and mixtures rich in carbon dioxide. It will be understood that the invention can be applied to cold-held devices other than by biberonnage and that even for a bottle-fed device, the storage of liquid is not necessarily inside the chamber. The positioning of the units shown in the figure is only an example and the units can be arranged differently. Similarly, the spatial arrangement of the elements inside the enclosure does not necessarily represent the physical reality. For example, the trading line may be next to the column or above the column. In particular, at least one fluid treatment element mounted on an outer wall of the enclosure is a separate fluid treatment element other than an exchanger.
Claims (11)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0755699A FR2917490A1 (en) | 2007-06-12 | 2007-06-12 | Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0755699A FR2917490A1 (en) | 2007-06-12 | 2007-06-12 | Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| FR2917490A1 true FR2917490A1 (en) | 2008-12-19 |
Family
ID=39273155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FR0755699A Withdrawn FR2917490A1 (en) | 2007-06-12 | 2007-06-12 | Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure |
Country Status (1)
| Country | Link |
|---|---|
| FR (1) | FR2917490A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2958026A1 (en) * | 2010-03-23 | 2011-09-30 | Air Liquide | Air separator of transport container, has support element that is extended in direction of main axis to locate auxiliary element between bottom portion of cooling box and edge portion of support element in main axis direction |
| CN110360811A (en) * | 2019-06-28 | 2019-10-22 | 上海二十冶建设有限公司 | The integrated installation method of overall skid-mounted formula ice chest |
| CN111981249A (en) * | 2019-05-22 | 2020-11-24 | 乔治洛德方法研究和开发液化空气有限公司 | Insulated enclosures containing equipment intended to operate at temperatures below 0°C |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1576945A (en) * | 1967-08-25 | 1969-08-01 | ||
| US5412954A (en) * | 1992-09-16 | 1995-05-09 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Precedes Georges Claude | Apparatus for cryogenic treatment, such as air distillation |
| JPH08261644A (en) * | 1995-03-23 | 1996-10-11 | Daido Hoxan Inc | Apparatus for producing high-purity nitrogen gas |
| US6378331B1 (en) * | 1997-11-17 | 2002-04-30 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Cold box for cryogenic distilling plant |
| US20040050095A1 (en) * | 2002-08-08 | 2004-03-18 | Brigham William D. | Nitrogen generator |
| US20060260357A1 (en) * | 2003-03-31 | 2006-11-23 | Air Products And Chemicals, Inc. | Apparatus for cryogenic air distillation |
-
2007
- 2007-06-12 FR FR0755699A patent/FR2917490A1/en not_active Withdrawn
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1576945A (en) * | 1967-08-25 | 1969-08-01 | ||
| US5412954A (en) * | 1992-09-16 | 1995-05-09 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Precedes Georges Claude | Apparatus for cryogenic treatment, such as air distillation |
| JPH08261644A (en) * | 1995-03-23 | 1996-10-11 | Daido Hoxan Inc | Apparatus for producing high-purity nitrogen gas |
| US6378331B1 (en) * | 1997-11-17 | 2002-04-30 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Cold box for cryogenic distilling plant |
| US20040050095A1 (en) * | 2002-08-08 | 2004-03-18 | Brigham William D. | Nitrogen generator |
| US20060260357A1 (en) * | 2003-03-31 | 2006-11-23 | Air Products And Chemicals, Inc. | Apparatus for cryogenic air distillation |
Non-Patent Citations (2)
| Title |
|---|
| "OXYGEN-NITROGEN GENERATORS", PUBLICATION BOC CRYOPLANTS, BOC CRYOPLANTS ENGINEERING CENTRE, GUILDFORD, GB, May 1992 (1992-05-01), pages 1 - 5, XP001223905 * |
| WINKLER D: "NEUE TECHNISCHE LOESUNGEN BEI KLEINEN LUFTZERLEGERN", LINDE SYMPOSIUM, XX, XX, October 1980 (1980-10-01), pages I,1 - 14, XP001182512 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2958026A1 (en) * | 2010-03-23 | 2011-09-30 | Air Liquide | Air separator of transport container, has support element that is extended in direction of main axis to locate auxiliary element between bottom portion of cooling box and edge portion of support element in main axis direction |
| CN111981249A (en) * | 2019-05-22 | 2020-11-24 | 乔治洛德方法研究和开发液化空气有限公司 | Insulated enclosures containing equipment intended to operate at temperatures below 0°C |
| EP3742094A1 (en) * | 2019-05-22 | 2020-11-25 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Thermally insulated enclosure containing a device to operate at a temperature below 0°c |
| FR3096442A1 (en) * | 2019-05-22 | 2020-11-27 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Thermally insulated enclosure containing equipment that must operate at a temperature below 0 ° C |
| CN110360811A (en) * | 2019-06-28 | 2019-10-22 | 上海二十冶建设有限公司 | The integrated installation method of overall skid-mounted formula ice chest |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2124898A1 (en) | Air distillation apparatus | |
| EP2972189B1 (en) | Gas-line probe adapter for connecting vacuum jacketing | |
| CA2491675A1 (en) | Thermally isolated conduit | |
| US8240167B2 (en) | Cryogenic freezing apparatus | |
| JP3436394B2 (en) | Low temperature processing equipment such as air rectification | |
| BRPI0519906A2 (en) | liquid-vapor separator, and, method for promoting uniform refrigerant flow | |
| FR2917490A1 (en) | Cold box for air separation apparatus, has air cleaning unit, separated fluid processing element or air compression unit separated in distillation column, where elements are mounted on external wall of enclosure | |
| US20020060274A1 (en) | Support for pipelines and process for mounting such a support | |
| US9841228B2 (en) | System and method for liquefying a fluid and storing the liquefied fluid | |
| US11319845B1 (en) | Crankcase ventilation system | |
| FR3133076A3 (en) | Hydrogen liquefaction apparatus | |
| CN102175457A (en) | Flat-shaped liquid-nitrogen and liquid-helium dual-media compatible heat sink device and cooling method thereof | |
| EP2800615B1 (en) | Low-temperature distillation separating apparatus and separating method using such an apparatus | |
| US12215680B2 (en) | Portable, cryogenic fluid pump apparatus with associated instrumentation, conduit legs and accessories | |
| CN212178200U (en) | Elbow for LNG return gas and liquid inlet | |
| FR3121744A3 (en) | Module to be incorporated in an air distillation installation | |
| FR3146725A3 (en) | Apparatus for separating a gas mixture by cryogenic distillation | |
| RU41982U1 (en) | FIRE FIGHTING PLANT | |
| WO2025119513A1 (en) | Installation for producing a cryogenic fluid | |
| WO2007011220A2 (en) | Module assembly for a gas system | |
| FR2906878A1 (en) | Nitrogen supplying method, involves sending liquid nitrogen towards separating apparatus for partially maintaining cooling of apparatus, during operating period, and conveying liquid nitrogen flow to vaporizer during another period | |
| US8955339B2 (en) | Cryogenic pump with a device for preventing the memory effect | |
| FR2920864A1 (en) | APPARATUS AND METHOD FOR TRANSFERRING A CRYOGENIC LIQUID | |
| WO2018206886A1 (en) | Heat exchange apparatus | |
| FR2846077A1 (en) | Heat exchange apparatus upstream of cryogenic gas distillation plant has outlet to extract first flow from intermediate level in first body |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| ST | Notification of lapse |
Effective date: 20100226 |