EP3465036A1 - Élément de construction d'un appareil d'échange de masse et/ou de chaleur, assemblage de deux éléments et procédé d'échange utilisant un assemblage - Google Patents
Élément de construction d'un appareil d'échange de masse et/ou de chaleur, assemblage de deux éléments et procédé d'échange utilisant un assemblageInfo
- Publication number
- EP3465036A1 EP3465036A1 EP17733500.7A EP17733500A EP3465036A1 EP 3465036 A1 EP3465036 A1 EP 3465036A1 EP 17733500 A EP17733500 A EP 17733500A EP 3465036 A1 EP3465036 A1 EP 3465036A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- chamber
- box
- modular
- assembly
- elements
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
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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
- F25J3/0295—Start-up or control of the process; Details of the apparatus used, e.g. sieve plates, packings
-
- 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
- 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
- F25J3/04969—Retrofitting or revamping of an existing air fractionation unit
-
- 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
- F25J2290/30—Details about heat insulation or cold insulation
-
- 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
Definitions
- the present invention relates to a modular element for the construction of a mass exchange apparatus. and / or heat, an assembly of at least two such modular elements and a method of mass exchange and / or heat with such an assembly.
- the invention also relates to an apparatus constituted at least partially by such an assembly of at least two such modular elements.
- the present invention relates in particular to a cryogenic distillation apparatus, such as an air separation, constituted at least partially by an assembly of modular elements according to the invention and to a method of modifying such an apparatus.
- the invention is also applicable to other mass and / or heat exchange apparatus, such as a heat exchanger, an adsorption purification apparatus or a distillation column.
- the apparatus according to the invention can be installed and commissioned quickly. Once installed, it is easy to increase or decrease its capacity and / or energy efficiency. Its maintenance is less complicated and if necessary, it is easy to move. In addition, it is easy to modify the apparatus according to the invention by modifying its capacity and / or the contents of the products it must produce. You can also add or remove a product.
- an air separation apparatus can be composed of a plurality of packets, each containing an entire equipment of the apparatus, for example the whole of a column, the whole of a heat exchanger, the whole of an adsorption unit for purification at the top of the air.
- the dimensions of each packet are determined by the equipment that it must contain and therefore the packages all have different dimensions. Most packages are placed directly on the ground.
- EP2657633 discloses a modular element in which two heat exchange bodies are arranged in an isolated enclosure. Both bodies have small openings on their upper surface to allow the passage of a pipe.
- An object of the invention is to facilitate the configuration of an apparatus for treating a gas, for example a waste gas from an industrial process or an apparatus for separating air by cryogenic distillation or a part thereof. apparatus.
- a gas for example a waste gas from an industrial process or an apparatus for separating air by cryogenic distillation or a part thereof. apparatus.
- the device can be built faster and with low skilled labor.
- a modular element containing a defective element can be replaced easily without the need to replace the entire equipment.
- a stackable modular element of construction of a mass exchange apparatus and / or heat comprising a parallelepipedic box having a length, a width and a height, the box having a face horizontal opposite upper and lower face, two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the box being defined by the length and the width of the box, the two front faces of the box by the length and the height of the box and the two lateral faces of the box by the width and height of the box, the box containing at least one layer of thermal insulation of thickness less than one third of the width of the box, the layer of insulating coating at least the lateral and front faces of the box and optionally the upper and lower faces and surrounding at least one parallelepiped-shaped chamber inside the box, the at least one chamber having a length, a width and a height, the chamber having a horizontal opposite upper and lower face, the upper face and / or the lower face of the chamber being at least partially open, two opposite vertical face faces and two opposite vertical
- the at least one body fills at least part of the chamber inside the casing and
- At least one material transfer line passes through the other part, or the remainder of the chamber or another chamber, to allow the material to pass through the casing or
- the other part or the rest of the chamber or the other chamber is a means for the transfer of material through the box.
- the height of the element is less than the length of the element, or even less than or equal to the width of the element.
- the height of the body is equal to at least half the height of the element, if not equal to the height of the element.
- At least one body is a body of adsorbent material.
- At least one body is constituted by a stack of vertically oriented metal plates, the plates being separated by fins.
- At least one body is constituted by a stack of vertically oriented corrugated plates, the corrugations being oriented at an angle between 10 ° and 80 ° with the horizontal.
- the dimensions of the modular element are chosen to correspond to an element size belonging to the range.
- the chamber is open on the upper face and the lower face of the box and the height of the chamber is substantially equal to the height of the box.
- the chamber is open on the upper face or the lower face of the box and closed on the opposite side thereof.
- At least one of the vertical faces of the box is in the form of a flat surface.
- At least the upper face and / or the lower face of the box comprises connecting means for making a connection between neighboring elements.
- the at least one chamber has a horizontal section of substantially square, rectangle or circular shape.
- the chamber has a uniform horizontal section over the entire height of the chamber.
- the chamber is closer to a side wall of the box that the opposite side wall of the box.
- the box is metal, preferably aluminum or stainless steel or carbon steel or Invar.
- the walls of the at least one chamber are metal, preferably aluminum or stainless steel or Invar.
- the element is self-supporting.
- the element has a length between 3 and 30 meters
- the element has a height between 1 and 5 meters
- the element has a width between 1 and 5 meters
- the thickness of the insulation layer is less than 500 mm, or less than 300 mm, or less than 150 mm or even 100 mm.
- the volume of the room or rooms constitutes at least 30% of the volume of the element.
- the element comprises four vertical beams connecting the upper face of the box to the underside of the box by the corners, so that the mechanical forces pass through the corners of these faces.
- the box is constituted by a standardized container, preferably having standardized corners, for example according to the ISO 668 standard
- an opening in the upper face of the chamber communicates with an opening in the upper face of the box, the two openings preferably having substantially the same dimensions.
- an opening in the lower face of the chamber communicates with an opening in the lower face of the box, the two openings preferably having substantially the same dimensions.
- the opening in the lower face and / or the upper face of the box occupies at least 20% of the surface of the respective face of the box.
- the opening in the lower face and / or the upper face of the chamber occupies at least 20% of the surface of the respective face of the chamber, preferably the entire surface of the respective face of the chamber.
- the box of the first element has the same length and width as that of the second element.
- the chamber of the first element has the same length and width as that of the second element.
- the center points of the first element chambers and the second element are on a common vertical axis.
- the body of the first element has the same length and width as that of the second element.
- the at least one material transfer line passes through the other part, or even the rest of the chamber or another chamber, to allow the material to pass through the casing of the first element and / or
- the other part, or even the rest of the chamber or the other chamber is a means for the transfer of material through the box of the first element.
- the at least one material transfer line passes through the other part, or even the rest of the chamber or another chamber, to allow the material to pass through the second element casing and / or
- the other part, or even the rest of the chamber or the other chamber is a means for the transfer of material through the box of the second element.
- the material transfer line of the first element is connected to the material transfer means of the second element, which means may be the material transfer line of the second element, or even a part of the chamber or another chamber of the second element;
- the other part or the remainder of the chamber or the other chamber of the first element is connected to the material transfer means of the second element, this means possibly being the material transfer line of the second element, or even a part of the room or another room of the second element
- the material transfer pipe of the first element is the transfer pipe of the second element
- a material transfer pipe passes through the first and second elements, or even most or all the elements of the assembly
- the assembly comprises at least one means of circulating at least one fluid or electricity from one element to another through at least one pipe, which may be a cable, or a chamber of each element
- the elements are fixed to one another by connecting the lower edges of the four lateral and front walls of the box of the first element to the upper edges of the four lateral and front walls of the box of the second element, by welding and / or adhesion using a seal and / or an adhesive and / or a mechanical attachment, with the possible use of a seal, preferably only by the corners, the assembly thus produced possibly providing a seal.
- the assembly comprises a third element in contact with the first or the second element, the third element being parallelepipedal having a length, a width and a height, the third element having a horizontally opposite upper and lower face, two end faces; vertical opposites and two opposite vertical lateral faces, the upper and lower faces of the third element being defined by the length and the width of the modular element, the two end faces of the modular element by the length and the height of the third element and the two faces lateral elements of the modular element by the width and height of the third element, the third element containing no element allowing the exchange of material as described in claim 3 but containing at least one cable and / or at least one pipe for transferring electricity or a fluid of the first or second me element.
- an apparatus for treating a gas for example an apparatus for separating air by cryogenic distillation in which:
- a gas purification unit for example air is at least partially constituted by an assembly of at least two elements as described above, the adsorbent is capable of adsorbing water and and / or carbon dioxide and / or a part of the secondary impurities in the air, the assembly comprising means for sending gas therefrom, for example air, to be purified with water and / or bound carbon dioxide to an element of the assembly and means for withdrawing purified gas from another element of the assembly and / or
- a heat exchanger is at least partially constituted by an assembly of at least two elements as described above, the assembly comprising means for sending a gas, for example air or a gas of the air, to an element of the assembly and means for withdrawing the gas at a warmer or cooler temperature from another element of the assembly and / or
- a distillation column is at least partially constituted by an assembly of at least two elements as described above, the assembly comprising means for sending a gas, for example air or a gas of air, connected to an element of the assembly and means for taking a purified gas or enriched in a gas component of another element of the assembly.
- a method of mass exchange and / or heat in an assembly or apparatus as described above in which at least one first fluid is introduced into the body of an element of an assembly and removing a second fluid derived from the first fluid of the body of another element of the assembly.
- the exchange of mass and / or heat takes place at a pressure of less than 2 bar, preferably at a pressure at most equal to 400 mbar above atmospheric pressure.
- At least some functional parts of the gas treatment apparatus are formed at least partially, preferably entirely, by modular elements.
- the entire apparatus may be composed of modular elements.
- an assembly of at least a first, a second and a third modular stackable elements of construction of a mass exchange apparatus and / or heat each of the first and second element comprising a parallelepipedic box having a length, a width and a height, the box having an opposite horizontal top and bottom face, two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the box being defined by the length and the width of the box, the two front faces of the box by the length and the height of the box and the two lateral faces of the box by the width and the height of the box, the box containing at least one layer of insulation thermal thickness less than one third of the width of the box, the layer of insulation coating at least the side and front faces of the ca isson and possibly the upper and lower faces surrounding at least one parallelepiped-shaped chamber inside the box, the at least one chamber having a length, a width and a height, the chamber having a horizontal opposite upper and lower face , the upper face and / or the lower face
- the at least one body fills at least part of the chamber inside the casing of the first and / or second element and
- At least one material transfer line passes through the other part, or the remainder of the chamber or another chamber, to allow the material to pass through the casing or iii) the other part or the rest of the chamber or another chamber is a means for the transfer of material through the box.
- At least one body is a body of adsorbent material and / or
- At least one body is constituted by a stack of vertically oriented metal plates, the plates being separated by fins and / or
- At least one body is constituted by a stack of corrugated plates oriented vertically, the corrugations being oriented at an angle between 10 ° and 80 ° with the horizontal.
- the first element contains a body as described in variant i) or ii) or iii) of claim 3 and the second element contains a body as described in variant i) or ii) or iii) of claim 3 .
- the third element contains no body as described in variants i), ii) or iii) of claim 3.
- the first element has the same length and / or width and / or height as the second element.
- the first, second and third elements are arranged with their lengths arranged in the same direction.
- the sum of the lengths of the first and second elements is less than, equal to or greater than the length of the third element.
- the first and second elements are arranged with their lengths arranged in the same direction and the third element is arranged with its length perpendicular to the lengths of the first and second elements.
- the sum of the widths of the first and second elements is substantially equal to the length of the third element.
- n third elements are disposed below or above the first and second elements, each third element being in contact with the first and the second element and each of the first and second elements comprising n openings to allow fluid transfer from / to to each of the third elements.
- the length of the first and / or second element is substantially equal to the sum of the widths of the third elements, preferably each third element having the same width and the length of the first and / or second element being substantially equal to n times the width of a third element.
- the third element has a height greater or smaller than the height of the first and / or second element.
- the third element is fixed on the ground.
- the casing of the third element contains at least one layer of thermal insulation with a thickness less than one-third of the width of the box, the layer of insulation coating at least the lateral and front faces of the box and optionally the upper and lower faces surrounding at least one chamber with parallelepipedal volume inside the box,
- the third element contains at least one chamber having a length, a width and a height, the chamber having a horizontal opposite upper and lower face, the upper face and / or the lower face of the chamber being at least partially open ( s), two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the chamber being defined by the length and width of the chamber, the two end faces of the chamber by the length and height of the chamber. the chamber and both sides of the chamber by the width and height of the chamber,
- a chamber of the third element contains at least one body of material allowing the exchange of mass and / or heat, the body being of parallelepipedal shape and filling at least a part of the chamber, the first and second elements each having the chamber having an opening on the upper face communicating with an opening in the upper face of the box and an opening on the lower face communicating with an opening in the underside of the box respectively to allow the transfer of fluid to the body from the outside of the box; element and / or body to the outside of the element
- the third element contains means for transferring at least one fluid from the first element to the second element and / or from the second element to the first element.
- the third element contains at least one duct and / or at least one duct, one end of which is connected to at least one body and / or at least one transfer duct of the first element and the other end is connected to at least one duct; body and / or at least one transfer line of the second element.
- the at least one pipe and / or the at least one sheath is coated with insulation the at least one duct and / or the at least one duct is coated with insulation is disposed in insulation which fills the space inside the third element
- At least the front and side faces of the third element are coated with an insulating layer
- the third element contains means of control and / or control and / or analysis and / or instrumentation and / or provision of utilities.
- the box of the third element contains on at least one side at least one layer of thermal insulation of thickness at least possibly less than one third of the width of the box.
- the first and / or second element constitutes the lower or upper element of a stack of elements, each element of the stack comprising a parallelepipedic box having a length, a width and a height, the box having an upper surface and a opposite horizontal bottom face, two opposite end faces vertical and two opposite vertical side faces, the upper and lower faces of the box being defined by the length and width of the box, the two front faces of the box by the length and height of the box and the two side faces of the box by the width and height of the box.
- At least one element of the stack is a support element that does not comprise openings for allowing the entry or the exit of a fluid.
- the box contains at least one layer of thermal insulation of thickness less than one third of the width of the box, the layer of insulation coating at least the lateral and front faces of the box and optionally the upper and lower faces and surrounding at least one parallelepiped-shaped chamber inside the box, the at least one chamber having a length, a width and a height, the chamber having a horizontal opposite upper and lower face, the upper face and / or the lower face of the chamber being at least partially open, two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the chamber being defined by the length and the width of the chamber, the two front faces of the chamber by the length and height of the chamber and the two side faces of the chamber by the wide ur and the height of the chamber, the chamber containing at least one body of material allowing the exchange of mass and / or heat, the body being of parallelepipedal shape and filling at least a portion of the chamber.
- each element of the cell or most elements of the cell contains a body composed of only one of the variants
- the third element comprises openings in only one face which is the upper face or the lower face.
- the third element comprises at least two openings in one of the faces which is the upper face or the lower face and at least one opening in the opposite face.
- the first and / or second element constitutes the lower or upper element of a stack of elements, connected by the first and / or second element to a first third element and also connected to a second third element arranged at an intermediate point; from the stack or at the other end of the stack
- each assembly being according to one of the preceding claims wherein the third element of one of the assemblies is connected to the third element of another assembly to through a fourth element comprising a parallelepipedic box, placed in contact with the third elements to allow the transfer of fluid from one assembly to the other through the fourth element and the third elements.
- an apparatus for treating a gas for example an apparatus for separating air by cryogenic distillation in which:
- a gas purification unit for example air is at least partially constituted by an assembly according to claim 3 variant i), the adsorbent is capable of adsorbing water and / or carbon dioxide; carbon and / or a part of the secondary impurities of the air, the assembly comprising means for sending gas therefrom, for example air, to be purified with water and / or carbon dioxide connected to an element of the assembly and means for withdrawing purified gas from another component of the assembly and / or
- a heat exchanger is at least partially constituted by an assembly according to claim 3 variant ii), the assembly comprising means for sending a gas, for example air or an air gas, to an element the assembly and means for withdrawing the gas at a warmer or cooler temperature from another component of the assembly and / or
- a distillation column is at least partially constituted by an assembly according to claim 3, variant iii) the assembly comprising means for sending a gas, for example air or an air gas, connected to an element of the assembly and means for withdrawing purified or enriched gas into a gas component of another element of the assembly.
- a gas for example air or an air gas
- a method of mass exchange and / or heat in an assembly or apparatus as described above in which at least one first fluid is introduced into the body of an element of an assembly and removing a second fluid derived from the first fluid of the body of another element of the assembly.
- the exchange of mass and / or heat operates at a pressure of less than 2 bar, preferably at a pressure at most equal to 400 mbar above atmospheric pressure.
- a method of constructing or modifying an apparatus for exchanging material and / or heat comprising an assembly at least first and second stackable modular elements, each of the first and second elements comprising a parallelepipedic box having a length, a width and a height, the box having an opposite upper and lower face horizontal, two opposite end faces vertical and two opposite sides vertical sides, the upper and lower faces of the box being defined by the length and width of the box, the two front faces of the box by the length and height of the box and the two side faces of the box by the width and height of the box, the box containing at least one layer of thermal insulation of thickness less than one third of the width of the box , the insulating layer coating at least the lateral and front faces of the box and optionally the upper and lower faces and surrounding at least one parallelepiped-shaped chamber inside the box, the at least one chamber having a length, a width and a height, the chamber having a horizontal opposite upper and lower face,
- the first element is fixed on the second element or the second element is fixed under the first element in a sealed manner, so that a fluid can pass from the body of the first element to the body of the second element and / or the body of the second element; element to the body first element and / or
- the first element is detached from the second element, above which it is sealed or the second element is detached from the first element below which it is sealingly attached, so that a fluid can pass from the body of the first element; element to the body of the second element and / or the second element to the body of the first element.
- the body of the first element and the body of the second element are both i) a body of adsorbent material or
- the at least one body fills at least part of the chamber inside the casing of the first and / or second element and
- the other part or the rest of the chamber or the other chamber is a means for the transfer of material through the box.
- the assembly constitutes at least part of an adsorbent bed, a heat exchanger or a distillation apparatus, preferably cryogenic, and in that
- the addition of the second element makes it possible to increase the capacity of the assembly and / or to increase the efficiency of the assembly or
- removal of the second element reduces the capacity of the assembly and / or reduces the efficiency of the assembly and / or reduces the volume of the assembly
- the first and / or second element constitutes element (s), possibly a lower or upper element, of a stack of at least two elements, each element of the stack comprising a parallelepipedic box having a length, a width and a height, the box having a horizontally opposite upper and lower face, two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the box being defined by the length and width of the box. box, the two front faces of the box by the length and height of the box and the two lateral faces of the box by the width and height of the box, most elements, or even each element, of the stack having the same width and possibly the same length and / or height.
- At least one element of the stack may be longer than other elements of the stack, preferably longer than most, if not all, elements of the stack
- the first element is removed and the first element is replaced by another element having the same type of body, i) ii) or iii) as described in claim 3 that the first body, but having a greater capacity and / or better efficiency and / or operation less defective than that of the first element.
- the first element is removed and replaced by a parallelepiped shaped element having the same length and the same width as the first element but not containing a body of the same type as the first body, or even not containing body of a type i) to iii) described in claim 3.
- a first stack is assembled comprising principally body elements of the type i) or of the type ii) or of the type iii) as described in claim 3 and a second stack is assembled comprising mainly body elements of the type i) or the type ii) or type iii) as described in claim 3 so that a side face of the second stack is substantially in contact with a side face of the first stack.
- a third battery is assembled comprising mainly body elements of the type i) or of the type ii) or type iii) as described in claim 3 so that a side face of the second stack is substantially in contact with a face side of the third stack.
- the first stack mainly contains body elements of type i) and / or the second stack mainly contains body elements of type ii) and / or the third stack contains mainly body elements of type iii).
- An element of the first battery or the second battery contains an air compressor for supplying air elements of the type body stack i) or ii).
- the first and / or second element is taken from a manufacturing center or a logistics platform and / or
- the first and / or second element is deposited in a manufacturing center or a logistics platform
- the manufacturing center or the logistics platform preferably containing several elements identical to the first element and / or several elements identical to the second element.
- a first and / or second element of a first apparatus is detached according to step b) above, the uncoupled element is deposited in a manufacturing center or a logistics platform, if necessary it is repackaged therein. disconnected element, we take the uncoupled element in the center or the platform to transport it to a second device where it is fixed in step a) above to another element to form part of the second device
- the invention proposes to use modular elements that make it possible to assemble and start up a gas treatment apparatus, for example an air separation apparatus, quickly, the modular elements being manufactured in accordance with the invention. workshop and being easily transportable sizes, typically the size of a standardized maritime container.
- the modular elements are easily joined together, to facilitate the construction of a device and are also easily detached to facilitate the modification or removal of the elements.
- connections of fluid or electricity or instrumentation may be made by means disposed on the outer walls of the adjacent or non-adjacent modular elements.
- the modular aspect makes it possible to increase or reduce the size of the apparatus for treating a gas, for example an air separation device, and also to easily disassemble it for installation on another site by adding or removing modular elements of modular elements within the same device.
- the modular aspect also makes it possible to easily multiply the number of devices in parallel (notion of "multi-train").
- Some modular elements may possibly be changed during the life of the device, for example by a modular element more energy efficient (but certainly more expensive) if the energy cost becomes greater.
- This configuration method can also be applied to an adjustment of the productions of liquid, of gas under pressure ...
- a single size of modular element having given dimensions to install part of a piece of equipment of the apparatus, using multiple modular elements each of the same size.
- two modular element sizes can be chosen, the modular elements of the two sizes each having the same height and the same width but the length of a modular element size being twice that of the other modular element size.
- a number of modular elements of a first size and a number of modular elements of a second size will be used.
- the dimensions are chosen so that at least one piece of equipment of the apparatus is not only transported on site in the modular element but installed on site to form part of the apparatus that operates, remaining inside the same modular element than that used for transport.
- a whole equipment of a device can enter a modular element, for example the equipment can be a reboiler or a condenser, a heat exchanger, for example a heat exchanger more small, such as a subcooler, a pump, a compressor, a turbine, a relief valve or a control room, instrumentation or electrical.
- the equipment can be a reboiler or a condenser, a heat exchanger, for example a heat exchanger more small, such as a subcooler, a pump, a compressor, a turbine, a relief valve or a control room, instrumentation or electrical.
- the equipment in working order is high, it is necessary to design the equipment in a series of pieces, each of which is arranged in an individual modular element.
- the modular elements are then superimposed and the pieces connected in series inside the modular elements to allow operation of the pieces in series, with at least one fluid of a modular element passing through the other modular element.
- the superimposed pieces make up the entire equipment, such as a column allowing the exchange of heat and / or material, for example a distillation column or a washing column or a heat exchanger or an adsorption tower or absorption.
- the height of the piece is chosen so that the piece can enter the modular element.
- the modular element is arranged with its length parallel to the ground, its width also parallel to the ground and its height being perpendicular thereto.
- the length of the modular element is preferably at least 1.5 times the height of the modular element, or even at least twice the height of the modular element , or at least 4 times the height of the modular element.
- the length of the modular element is preferably at least 1.5 times the width of the modular element, or even at least twice the width of the modular element , or at least 4 times the width of the modular element.
- the width of the modular element may be greater or smaller than the height of the modular element or equal to it.
- the length of the modular element is obviously larger than the height of the modular element and greater than its width.
- the length of the shorter modular element is preferably at least 1.25 times the height of the modular element shorter, or even at least 1.5 times the height. shorter modular element, or at least twice the height of the shorter modular element.
- the length of the longer modular element is preferably at least 2.5 times the height of the modular element longer, or even at least 3 times the height of the modular element longer, or at least 4 times the height of the longer modular element.
- the length of the shorter modular element is preferably at least 1.25 times the width of the modular element shorter, or even at least 1.5 times the width. shorter modular element, or at least twice the width of the modular element shorter.
- the length of the longer modular element is preferably at least 2.5 times the width of the modular element longer, or at least 3 times the width of the modular element longer, or at least 4 times the width of the longer modular element.
- the shortest modular element and the longest modular element have the same height and width.
- the height of the longer modular element is half the height of the shorter modular element and / or the length of the longer modular element is substantially the same. double the length of the shorter modular element.
- the modular elements can be declined according to different configurations.
- the modular elements may each contain a portion of equipment having only one main function.
- equipment such as a heat exchanger
- equipment may consist of part or all of superimposed modular elements.
- An adsorption purification apparatus may consist partly or entirely of superimposed modular elements.
- a distillation or washing column may consist partly or entirely of superposed modular elements.
- a modular element may not contain instrumentation or power supply and in this case does not necessarily require validation / test workshop, other than quality control.
- a modular element can contain objects having a multitude of functions (rotary machines, such as a compressor, a turbine or a pump, electrical components, instrumentation, processes, fluid distribution devices (pipes , valves %), becoming a complex module that requires a validation / test / complete control in the workshop
- the modular element can contain equipment having an "annex" function such as support, control room, electrical room, instrumentation / analysis room, store / spare room ...
- the modular elements can be arranged so that their length is arranged vertically and / or horizontally with respect to the ground, once set up to constitute the apparatus.
- the position with the length arranged horizontally relative to the ground when the element is installed at its final position is preferred for reasons of stability and ease of assembly of the elements.
- these elements are generally transported with their length in the horizontal direction, for example by truck or boat, the element remains in the same position for transport and final installation. It is therefore not necessary to provide supports inside the element to prevent its contents from moving when the element is in a vertical position, since the element is always in the horizontal position, whether it is for transport, on-site installation or final disposal on site.
- the structure of at least the modular elements in contact with sections of the apparatus operating at a subambient or even cryogenic temperature will be in a material that is mechanically resistant to low temperature or a more conventional material protected by adequate thermal insulation.
- the walls of the modular element will be flat, or “curved” outwards or inwards if it is easier to contain the pressure.
- the solution “convex” inward facilitates the transport (the wall does not exceed the "carrier” structure).
- the insulation may be integrated with the walls and structures exposed to the ambient environment, for example using vacuum panels.
- the use of more traditional insulation may also be provided according to the accessibility required for the maintenance of the equipment concerned.
- the wall of the inner zone with its possible insulation delimits a chamber and can directly "contain" the body having a process function (for example, exchange waves for heat exchange, structured packing for distillation, adsorbent for adsorption, compression, relaxation).
- Connectors for transferring at least one fluid between the modular elements can be made by welding or preferably by a mechanical system with a seal compatible with cryogenic temperatures and with the nature of the product to facilitate scalability and ease of disassembly , both at the level of the fluid distribution (“pipes”) or at a connection between two parts of the same process function.
- the mechanical strength of the assembly of the modular elements may, for example, be provided by a twist lock type system (in English “twist-lock”) preferably housing in the standardized corners of the modular element) regardless of the connection " fluid ", the connection” fluid "just ensuring a seal, which may be imperfect.
- a twist lock type system in English “twist-lock” preferably housing in the standardized corners of the modular element
- the modular elements have guides and quick locking systems in the corners, allowing precision in plug and play connections.
- the civil engineering can remain simple, using a single flat slab or only piles located under the structure, possibly only corners, of each modular element resting on the ground.
- the modular element resting on the ground can be possibly reinforced, for example, by adding point of contact with the ground.
- the modular elements preferably have a structure such that the mechanical forces between elements or the ground are preferentially taken up in the corners.
- the insulation of a modular element is integrated in the walls of the element and possibly in the structure of the element. This avoids the formation of thermal bridges.
- a modular element has at least one dimension, or even two or three, greater and / or at least one dimension, or even two or three, lower and / or at least one dimension, or even two or three, equal to those of a standardized container maritime.
- the modular element has at least one dimension corresponding to the size of a standard shipping container of 20 feet or 40 feet, or about 2.5 x 2.5 x 6 m or 2.5 x 2.5 x 12 m.
- An element can have at these eight angles a standardized wedge of maritime container, for example according to ISO 668.
- FIGS. 1, 3 and 4 represent modular elements according to the invention and FIG. 2 which shows two superimposed modular elements to form an assembly according to the invention
- FIGS. to 8 represent assemblies of modular elements according to the invention
- Figure 9 which shows a section of modular elements assembled according to the invention
- Figure 10 which shows a section of a modular elements according to the invention
- Figures 1 1 to 13 which represent assemblies of modular elements according to the invention
- Figures 14 to 19 which show a life cycle of an assembly of modular elements according to the invention.
- Figure 1a is a top view of a modular element. A view from below would be substantially identical.
- the modular element 10 is an element allowing an exchange of material and / or heat. It is composed of a box 2 of parallelepiped shape, formed of beams for example metal.
- the element has eight ISO 101 "container" wedges attached to the casing 2 and has a width oriented horizontally to the ground, a length oriented horizontally to the ground and a vertically oriented height from the ground, when it is installed to be part of a device.
- ISO containers are subject to specific building standards and performance tests. It's the same for ISO corners.
- ISO corners are certified by an internationally recognized organization to allow their "multimodal" use in maritime, road, rail or even air transport.
- ISO wedges made of steel, aluminum or stainless steel are commercially available for their specified purpose.
- the element comprises a box having a horizontal opposite upper and lower face, two opposite vertical end faces and two opposite vertical side faces, the upper and lower faces of the box being defined by the length and the width of the box, the two front faces of the box by the length and height of the modular element and the two side faces of the box by the width and height of the box.
- the side and front walls are for example sheet metal.
- the faces formed by the width and the length of the element are open to allow the passage of fluids.
- the opening may be smaller than the surface of the lower and / or upper face, covering at least a portion of the insulation 3 and possibly part of the zone 4.
- the height and the width of the element are not necessarily identical, so that the side walls can all be rectangular without being square.
- the walls may also be smaller than the dimensions of the element box.
- the walls are preferably fixed inside the box 2, but can be fixed outside thereof.
- An insulator 3 dresses the box 2 on the inner side, at least on the vertical sides of the parallelepiped.
- the upper and / or lower face may also comprise a wall, and be isolated.
- the insulator 3 can be plated on a sheet which rests on the casing 2 to ensure a "fluid" seal between the interior and the ambient.
- the insulator 3 can also directly provide this sealing function, as well as the structuring wall function.
- a sealed wall for example a metal sheet, may be applied on the inside of the insulator 3.
- the box 2 and the insulator 3 delimit an internal area.
- the casing 2, the wall and / or the insulation 3 may be sized to contain the possible overpressure inside the inner zone.
- the inner zone surrounds an area 4.
- This zone 4 contains a body which makes it possible to carry out mass and / or heat transfer, for example structured packing to make distillation, a plate and fin exchanger matrix for making heat exchange, adsorbent in the form of beads or structured to adsorb.
- This zone may also contain an area of the support, for example in the lower part, fluid distribution zones, for example in the lower part and / or in the upper part. It can also be partitioned into several parts, for example vertically, with walls that can be sealed, and / or structuring (for example, withstanding a differential pressure) and / or thermal insulators.
- the body fills the entire section of zone 4.
- At least one fluid flows upwards or downwards through zone 4.
- a fluid for example a gas
- another for example a liquid
- the inner zone may be entirely made up of zone 4. However, as illustrated, it may also also contain at least one other zone, for example here a fluid circulation zone 5, delimited by a leaktight and possibly insulating wall 6, in a kind of sheath.
- the part in contact with the insulator 3 may be delimited by a sealed wall, for example metal, if the insulation does not provide this function.
- two fluid circulation zones 5 are delimited by a vertical leaktight wall 6. This makes it possible to replace gas or liquid lines of a conventional apparatus by circulating at least one fluid to be sent to a modular element higher or lower and not to be treated by mass exchange and / or heat in the element through which they circulate.
- the inner zone comprises several zones 4.
- the at least two zones could each have a different function or different dimensions, one containing structured packings and the other a plate and finned exchanger matrix.
- the fluid sent into the zone 5 can be directly in contact with the walls of the zone, which separate the zone of the insulation. Otherwise the fluid can be contained in a pipe that passes through the area.
- Figure 1b shows a section on line X-X of Figure 1a. It shows the four beams of the box 2 and two of the side walls attached to the inside of the beams and coated with insulation 3.
- a mass exchange body and / or heat of the first zone 4 is held in place by the insulator 3 and is supported by a distributor 4 'for dispensing a gas passing from the outside of the element to the body or the body to the outside of the element.
- This distnbutor can also be used to hold the body in place.
- This distributor can be reduced to a set of support beams.
- the body may be a mass exchange body only, a heat exchange body only, (for example a plate and fin heat exchanger) or a mass and heat exchange body.
- Figure 1c shows a variant of the element with a section on line Y-Y of Figure 1a. It shows the four beams of the caisson 2 and two of the side walls attached to the inside of the beams and coated with insulation 3.
- a barrier 6 divides the chamber 5 in two to form two gas paths, one of the two paths being again divided in two by the barrier 6 ', the barriers 6, 6' forming a T.
- the gas rises or falls in the path coming from outside the element.
- Figure 1d shows a variant of the element of Figure 1c with a section on line Z-Z of Figure 1a.
- the body is divided into two parts 3, 4, each having a distributor and / or a set of beams support, down, the two parts being separated vertically from one another by a space.
- the gas rising in the path 5 next to the body 4 enters the body 3 through the distributor 3 '.
- Figure 2 shows a view on the side of an assembly of two modular elements according to Figure 1a. For each modular element, we see the four beams of the box and one of the side walls coated with insulation.
- the stack of two parallelepiped-shaped modular elements 10 and 20 forms an assembly of two modular elements interconnected by mechanical connection parts 141 at the ISO corners 101.
- the opening between the two parallelepiped-shaped modular elements, generated by the connecting piece 141 and / or by the spacing of the beams between the frames of the two modular elements, is filled by an element 131 which provides both the sealing vis-à-vis the outside and the continuity of the insulation between the two modular elements of parallelepipedal shape 10 and 20.
- the element 131 may be composed of several sub-elements, for example one ensuring the isolation function and another the sealing function.
- the connecting piece 141 may be made in such a way that the upper and lower ISO corners are in contact, for example, by an internal mechanical connection at the ISO or outside corners using the lateral holes of the ISO corners.
- the opening between the two parallelepiped-shaped modular elements is then reduced to its minimum, approximately 2 cm, corresponding to the positioning gap of the horizontal metal beams and the ISO corner 101, in general, around 1 cm.
- the two elements have the same length and the same width, it is sufficient to fix one element on the other by the corners 101 which are contiguous, in order to attach the elements together.
- the space between the elements is filled at least with the seal 131 so that the fluids in the zones 4 can not leave all the elements but pass entirely from one element to another.
- FIG. 3 represents a top view of a modular element according to FIG. 1a bearing the sealing element 131.
- This figure shows the location of the sealing element, for example a seal 131, at the interface between two parallelepiped-shaped modular elements 10, 20.
- the element 131 is based on the thickness of the insulation, and also preferentially on the caisson 2, with the exception of ISO 101.
- Other elements 132, 133 and 134, possibly of the same nature as the element 131, will ensure the continuity of fluids between the two modular elements of parallelepipedal shape 10, 20, in terms of sealing and possibly insulation: element 132 in the case where the zone 4 has been partitioned into several parts, for example vertically, with walls that can be sealed, the element 133 in the case where it is desired to channel a fluid leaving the zone 4, typically at the outlet of a heat transfer the element 134 for the fluid circulation zones 5.
- These elements 131, 132, 133 and 134 can be put in place during the assembly of the two parallelepiped-shaped modular elements 10, 20. These elements 131, 132, 133 and 134 may possibly constitute a single piece.
- FIG. 4 is a top view of a variant of FIG. 1a in which zone 4 does not contain a body which is only a part of a mass / heat transfer element but contains a complete equipment 7, for example example of heat transfer, which comprises for example an inlet 8 and an outlet 9, which pass through the insulation 3, the possible structuring wall and / or sealing, and possibly the structure 2.
- a complete equipment 7 for example example of heat transfer, which comprises for example an inlet 8 and an outlet 9, which pass through the insulation 3, the possible structuring wall and / or sealing, and possibly the structure 2.
- an element of a separation apparatus is sufficiently small or complex to be divided into several sections, each of which would be in a respective modular element. This is typically the case of heat exchangers used as reboilers or as condensers.
- At least one fluid flows upwards or downwards through the interface between two parallelepiped-shaped modular elements, at the level of the zone 4, the two parallelepiped-shaped modular elements being of the type shown in FIG. 4, or FIG. 1 a and Figure 4.
- a gas separation apparatus 1 for example air, is at least partly made up of different modular elements 1 1, 12, 21, 22, 23, 24, 31, 32, 33, 41 , 42, 43, 44, 45, 46, 47 and 48 as described for at least one of the preceding figures. They are of parallelepipedal shape and comprise at least 8 corners 101, for example ISO of container type, fixed on a structure, assembled for example as described above.
- the modular elements 1 1 and 12 may be dimensions of a standard container 40 feet long and the other modular elements
- the circulation of the fluids respectively in a first stack composed of the modular elements 21, 22, 23 and 24, a second stack composed of the elements modular 31, 32 and 33, a third stack composed of the modular elements 41, 42, 43, 44, 45, 46, 47 and 48 is essentially vertically within each modular element and each stack, and essentially vertically at the interface 1 1, 12 between two modular elements of the stack.
- Each stack is arranged so that the longest edge of the modular elements is parallel to the ground.
- the first stack 21, 22, 23 and 24 can essentially perform the function of pre-cooling and purification at the head, the second stack 31, 32 and 33 the exchange function and the third battery 41, 42, 43, 44, 45, 46, 47 and 48 the cryogenic distillation function between nitrogen and oxygen.
- the third stack could be a single column operating at low pressure or a plurality of columns at different pressures, each consisting of a few elements of the stack.
- the modular elements 1 1 and 12 make it possible in particular to circulate the fluids horizontally through rectangular ducts and / or round pipes so as to transfer the fluids respectively between the first stack 21, 22, 23 and 24 and the second stack 31, 32 and 33, the second stack 31, 32 and 33 and the third stack 41, 42, 43, 44, 45, 46, 47 and 48.
- the modular elements 1 1 and 12 can also provide process functions and / or controls and / or utilities. For example they may contain control means and / or control and / or analysis and / or instrumentation and / or supply of utilities, such as electricity or air instrument.
- the modular element 1 1 is placed astride the modular elements 24 and 33, above the first and the second stack, and the modular element 12 placed astride the modular elements 31 and 41 under the second and the third stack.
- the modular elements 1 1 and 12 preferably comprise intermediate ISO corners 102 to facilitate assembly respectively with the modular elements 24 and 33, with the modular elements 31 and 41.
- the modular element 1 1, 12 can be isolated in different ways. It can be isolated by depositing an insulator on the outside of the box. It can be insulated by coating the inside of the front and side insulation faces and in addition the upper or lower face if it is exposed. Another possibility is to isolate the at least one pipe or the at least one sheath inside the element 1 1, 12. As the elements 1 1, 12 comprise only two openings, these openings being in the lower face and the upper face respectively, the elements 1 1, 12 serve essentially to transfer a fluid from a stack to the adjacent stack, and possibly to change the flow direction of fluids passing through the stacks. Thus a fluid passing through the first stack from bottom to top can pass through the second stack from top to bottom. Note, however, that a fluid can cross the two batteries in the same direction. For example, a gas passes through the first stack and is sent to the second stack through the element 1 1. Then it goes down to the element 31 via the zone 5 of the elements 33, 32, 31 before being sent to the chamber of the element 31.
- the column thus formed would have a particularly small height.
- FIG. 6 differs from FIG. 5 by the addition of a fourth additional stack composed of modular elements 51, 52, 53, 54, 55, 56, 57, 58, 59, 60, 61 and 62, which in the case separation of air can essentially ensure the function of cryogenic distillation between argon and oxygen.
- the modular element 43 of Figure 5 has been replaced by the modular element 13 which allows in particular to circulate the fluids horizontally through rectangular ducts and / or round pipes so as to transfer the fluids respectively between the third stack 41 , 42, 44, 45, 46, 47 and 48 and fourth additional stack 51, 52, 53, 54, 55, 56, 57, 58, 59, 60, 61 and 62.
- the modular element 13 is placed within the third stack (between the modular element 42 and 44) and within the fourth additional stack (between the modular element 53 and 54).
- the modular element 13 makes it possible, if necessary, to circulate fluids vertically between the lower part of the third stack 41 and 42, and the upper part of the third stack 44, 45, 46, 47 and 48.
- the modular element 13 allows in this case to distribute the gas from a single stack on two batteries.
- a gas of an intermediate point of the third stack, constituting a simple low pressure distillation column is enriched in argon. This gas continues in part its way up the single column, that is to say elements 45 to 48 but is also sent up the fourth additional battery 54, 55, 56, 57, 58, 59, 60, 61 and 62.
- Elements 51 to 53 may have several variants. They can be simple supports in which case they do not even contain insulation, being simple empty boxes. They may contain other elements useful for the process, for example pumps.
- the elements 51 to 53 may be modular elements according to the invention as illustrated in Figures 1 to 4 with a chamber containing a distillation packing body. They may for example form a denitrogenation column, with the pipes containing the argon produced by the element 62 sent through the zones 5 of the elements 62 to 54, the element 13 and the zones 5 of the elements 51 being sent to the element 51 to be distilled therein and to provide a product rich in argon from the element 53.
- Figure 7a is a front view and Figure 7b is a rear view of the same assembly.
- the stacks of parallelepiped-shaped modular elements that have at least 8 container-type ISO 101 corners attached to a structure are contiguous along the length of the modular elements, instead of the width.
- the modular elements 21, 22, 23, 24, 31, 32, 33, 41, 42, 43, 44, 45, 46, 47 and 48 are of dimension of a container 20 feet. If the invention as directly described in Figure 5 (ie, to have a container that "overlaps" two containers of two adjacent stacks), the modular link elements 11 and 12 of The figure would have a width that is double that of a container format, which does not allow its transport and handling by conventional means.
- the horizontal connection between the first stack and the second stack, respectively the second stack and the third stack is made using two modular elements 1 1a and 1 1b, respectively 12a and 12b , the width and height being that of a conventional ISO container, and the length adjusted to two standard ISO container widths so as to properly associate with both Battery.
- This configuration allows its transport and handling by conventional means.
- connection between the first stack and the second stack could be achieved through a single modular element 11a, and that between the second stack and the third stack to a single modular element 12a, the modular element 12b can be reduced to its only function of structure.
- Figure 9 illustrates the connection between two batteries, for example the assembly 12 of Figure 5.
- the modular elements 31 and 41 are arranged on the modular connecting element 12 which is arranged on a non-illustrated support.
- the element 82 provides both external sealing and continuity of the insulation between the modular element 12 and the modular element 31, respectively 41, as described above.
- the element 71 symbolizes a fluid sheath (or a pipe) which makes it possible to pass from / to the modular element 31 towards / of the modular element 41 while passing substantially horizontally through the modular element 12, having a vertical transfer from / to the modular element 31, respectively the modular element 41 to / from the modular connecting element 12, the joining plane then being horizontal.
- the modular element 12 preferably has intermediate ISO corners 102 to facilitate assembly with the modular elements 31 and 41.
- Figure 10 illustrates (seen from above) an alternative to Figure 9 of a modular connecting element 12.
- the element 71 is a fluid sheath for moving from one stack to another.
- Element 72 is a fluid pipe for passing from one stack to another.
- the spaces 73 and 74 delimited by internal walls and the wall of the insulator 83 make it possible to pass fluids between the two stacks.
- the modular link element 12 may also contain process equipment: for example, a piece of process equipment 91, such as a material exchange and / or heat exchange body may be delimited by the insulation 83 and an inner wall, or another piece of process equipment 92 with its own container, by example a distillation column.
- the modular link element 12 can also also contain control functions, instrumentation and / or utilities.
- the modular element 12 preferably comprises intermediate ISO corners
- Figure 11 differs from Figure 5 by doubling the second stack into two parallel sub-stacks 31a and 32a, respectively 31b and 32b.
- the modular elements 12b and 11c allow fluids to be transferred to / from the two sub-stacks, from the modular elements 12a and 11b.
- Modular element 12c can be reduced to its sole function of structure.
- the modular element 1 1 a makes it possible to transfer fluids to / from the first stack 21, 22 and 23.
- the modular elements 11a, 11b, 11c, 12a, 12b and 12c may have the same height as the other modular elements, or preferably a reduced height for example by half, as shown in Figure 1 1.
- Figure 12 differs from Figure 1 1 by doubling the first stack into 2 parallel sub-stacks 22a and 23a, respectively 22b and 23b.
- the modular elements 11a and 21 make it possible to transfer fluids to / from the two sub-batteries.
- FIG. 13 differs from FIG. 5 in that the elements 21, 22, 23 and 24 are larger in size than the modular elements 31 -33 and 41 -48, for example containers 40 'and that the connecting element 1 1 has an intermediate size between 20 'and 40' so as to overlap the two piles 21 -24 and 31 -33.
- the battery 21 -24 has a different orientation from the other batteries, in particular the adjacent one 31 -33, preferably perpendicular.
- Figures 14 to 22 describe an example of a life cycle of an apparatus for separating and / or liquefying gas, for example air.
- the apparatus is constituted at least in part by different parallelepiped-shaped modular elements according to one of FIGS. 1 to 4. which comprises at least 8 ISO 101 container-type wedges fixed on a structure, assembled for example as described above. .
- Figure 14 illustrates the construction of the apparatus in its initial configuration.
- the various modular elements A, B, C, D, E, F, G, H, I, J, K and L are of two different sizes.
- the modular elements all have the same height and width.
- the modular elements C and E are substantially twice as long as the others.
- A, L and K may also be substantially twice as long as the others.
- the modular elements are superimposed on three vertical piles.
- Each stack consists only of elements of one of two sizes.
- the modular elements come from a manufacturing center CF and / or a logistics platform PL where several elements of each of the two sizes are stored. There are several copies of each element and each type of body, to replace any faulty element.
- a quality control process ensures that each modular element is functional,
- the various modular elements are assembled on site by stacking them to constitute at least a part of the apparatus.
- the first stack comprises an element A, surmounted by three elements B and a part of the element C.
- the modular element A may contain an air blower and a pre-cooling, the modular elements B of the adsorbent for purifying the air from the blower in A and the modular element C fluid transfer sheaths from the first stack to the second stack and / or the second stack to the first stack.
- the modular elements are designed so that the air rises from the lowest modular element B to the middle modular element B and then to the upper modular element B, purifying with water and carbon dioxide. carbon and some of the secondary impurities in the air. Then the purified air of the modular element B from the top is transferred to the sheaths of the modular element C to pass into the second stack. The regeneration nitrogen is transferred by the modular element C of the second stack to the modular elements B.
- the second stack is placed next to the first stack so that the side walls of the modular elements of the two stacks touch each other, possibly with a small day in between.
- the second stack comprises a portion of the modular element C containing the sheaths described above, the three modular elements D each containing a heat exchange section, and a portion of the modular element E containing sheaths for transferring to the at least one fluid from the second stack to the third stack and / or at least one fluid from the third stack to the second stack.
- the purified air passes through the modular elements D to be cooled to a cryogenic temperature and distillation fluids pass from the modular element E to the modular elements D to be heated.
- the third stack is placed next to the second stack so that the side walls of the modular elements of the two stacks touch each other, possibly with a small day in between.
- the third stack higher than the other two, comprises at the bottom part of the modular element E with its fluid transfer sheaths.
- E the modular element F which is a vaporizer.
- F are superposed the three modular elements G each containing a distillation section.
- the modular element H contains a condenser and optionally a distillation section and is above the lowest of the modular elements G.
- the three modular elements I each containing a distillation section.
- a condenser Above the highest section of the modular element I is a condenser.
- the modular element K which contains a heat pump for distillation
- the modular element L which contains a heat pump for the refrigeration balance of the apparatus.
- the installation of the device is limited to have the modular elements on top of each other and ensure that they are well attached and sealed to each other and that the battery is securely attached to the ground. This can be achieved by unskilled labor.
- Figure 15 illustrates a first evolution of the apparatus of Figure 14 during its life cycle.
- a new modular element I containing a distillation column section comes from a manufacturing center CF and / or a logistics platform PL. It is interposed between the upper modular element I and the modular element J, for example to increase the purity of a product. For this it is sufficient to remove the condenser J, to have the new modular element I in place of the condenser and replace the condenser J above the new modular element I. In this way, four modular elements I are superimposed instead three.
- the modular element I may contain a distillation section for the purpose of producing pure nitrogen ("minaret").
- a modular distillation element can be omitted.
- the added or removed modular element may also contain a liquid product pump, a liquefier or a product compressor.
- Figure 16 illustrates a maintenance of the apparatus of Figure 15 during its life cycle.
- a functional modular element L comes from a manufacturing center CF and / or a logistics platform PL and replaces the defective modular element L.
- the defective modular element L is returned to the manufacturing center CF and / or to a logistics platform PL where it can be repaired and made available, or dismantled, possibly recycling part of its components.
- FIG. 17 illustrates a second evolution of the device of Figure 15 during its life cycle.
- New modular elements J, F and K come from a manufacturing center CF and / or PL logistics platform and are interposed at different locations of the device, for example to increase the energy efficiency of the device.
- the energy consumption can for example be reduced on the one hand, by doubling the vaporizer by adding a modular element F and / or by doubling the condenser by adding a modular element J, to reduce the thermal nip of these exchangers, on the other hand, by doubling the heat pump for distillation by adding a modular element K, to operate the pump to heat with better performance.
- Figure 18 illustrates a third evolution of the apparatus of Figure 17 during its life cycle.
- New modular elements M, N, O and P come from a manufacturing center CF and / or from a logistics platform PL and are interposed at different locations of the apparatus, for example to produce another product.
- the new modular elements are arranged to form a fourth stack.
- the modular element M may contain transfer sheaths and is larger in size.
- the fourth battery comprises at the bottom the modular element P which contains a pump for raising liquid, then the three superposed modular elements O each containing a distillation section. Part of the modular element M, which is inserted in the third stack is above the upper modular element O. Then above the part of the modular element M present in the fourth stack, there is eight modular elements N superimposed each containing a distillation section.
- the head of the fourth stack is surmounted by a condenser H, moved from the third existing stack of Figure 17.
- Figure 19 shows the end of the cycle of the device.
- At least one of the modular elements A, B, C, D, E, F, G, H, I, J, K, L , M, N, O, P is returned to the manufacturing center CF and / or to a logistics platform PL where they can be either made available, or modernized or dismantled, possibly recycling part of their components.
- an item that is no longer required on a first device can be returned to the manufacturing center or the logistics platform, possibly stored on site and sent to a second device when an item need arises.
- This mode of operation has advantages of speed of intervention, economy of scale and ecological management.
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)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Separation Of Gases By Adsorption (AREA)
- Packages (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
Claims
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1655111A FR3052242B1 (fr) | 2016-06-06 | 2016-06-06 | Element de construction d’un appareil d’echange de masse et/ou de chaleur, assemblage de deux elements et procede d’echange utilisant un assemblage |
| FR1655112A FR3052243B1 (fr) | 2016-06-06 | 2016-06-06 | Assemblage d'elements modulaires de construction d'un appareil d'echange de masse et/ou de chaleur et procede d'echange utilisant un assemblage |
| FR1655113A FR3052244B1 (fr) | 2016-06-06 | 2016-06-06 | Procede de construction ou de modification d'un appareil d'echange de matiere et/ou de chaleur |
| PCT/FR2017/051383 WO2017212144A1 (fr) | 2016-06-06 | 2017-06-02 | Élément de construction d'un appareil d'échange de masse et/ou de chaleur, assemblage de deux éléments et procédé d'échange utilisant un assemblage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP3465036A1 true EP3465036A1 (fr) | 2019-04-10 |
| EP3465036B1 EP3465036B1 (fr) | 2020-09-16 |
Family
ID=59227762
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP17733500.7A Active EP3465036B1 (fr) | 2016-06-06 | 2017-06-02 | Élément de construction d'un appareil d'échange de matière et/ou de chaleur, assemblage de deux éléments et procédé d'échange utilisant un assemblage |
| EP17733503.1A Active EP3465037B1 (fr) | 2016-06-06 | 2017-06-02 | Procédé de construction ou de modification d'un appareil d'échange de matière et/ou de chaleur et appareil d'échange de matière et/ou de chaleur correspondant |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP17733503.1A Active EP3465037B1 (fr) | 2016-06-06 | 2017-06-02 | Procédé de construction ou de modification d'un appareil d'échange de matière et/ou de chaleur et appareil d'échange de matière et/ou de chaleur correspondant |
Country Status (5)
| Country | Link |
|---|---|
| US (2) | US11215395B2 (fr) |
| EP (2) | EP3465036B1 (fr) |
| CN (2) | CN109564059B (fr) |
| FR (3) | FR3052244B1 (fr) |
| WO (3) | WO2017212145A1 (fr) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR3074274B1 (fr) | 2017-11-29 | 2020-01-31 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Procede et appareil de separation d'air par distillation cryogenique |
| US11952769B2 (en) | 2018-03-02 | 2024-04-09 | Modular Plant Solutions Llc | Modular process plant structural system |
| FR3093008B1 (fr) * | 2019-02-21 | 2021-01-22 | Air Liquide | Installation et procédé de séparation des gaz de l’air à basse pression |
| FR3093169B1 (fr) * | 2019-02-21 | 2021-01-22 | Air Liquide | Installation et procédé de séparation des gaz de l’air mettant en œuvre un adsorbeur de forme parallélépipèdique |
| FR3093009B1 (fr) | 2019-02-21 | 2021-07-23 | Air Liquide | Procédé et installation de purification d’un flux gazeux de débit élevé |
| FR3096442B1 (fr) * | 2019-05-22 | 2021-05-21 | Air Liquide | Enceinte isolée thermiquement contenant un équipement devant fonctionner à une température en dessous de 0°C |
| FR3102238B1 (fr) * | 2019-10-16 | 2022-11-04 | Air Liquide | Enceinte de colonne de distillation cryogénique et procédé d’assemblage d’une telle enceinte |
| FR3111968B1 (fr) * | 2020-06-30 | 2022-05-20 | Air Liquide | Enceinte isolée thermiquement pour appareil de distillation cryogénique et procédé de transport et de construction d’une telle enceinte |
| FR3116892B1 (fr) * | 2020-12-02 | 2022-12-30 | Air Liquide | Appareil de séparation d’air par distillation cryogénique |
| DE102023202143A1 (de) * | 2023-03-10 | 2024-09-12 | Robert Bosch Gesellschaft mit beschränkter Haftung | ISO-Frachtcontainer und Adsorptionskammermodul für eine modulare CO2-Adsorptionsvorrichtung zum Trennen von CO2 |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1051622A (fr) | 1964-03-23 | |||
| DE2822774C2 (de) * | 1978-05-24 | 1982-08-26 | Linde Ag, 6200 Wiesbaden | Verfahren und Anlagenteile zum Errichten einer Fabrikanlage |
| US4872955A (en) | 1986-03-17 | 1989-10-10 | Uni-Frac Inc. | Vapor/liquid contact column structure |
| GB9503592D0 (en) * | 1995-02-23 | 1995-04-12 | Boc Group Plc | Separation of gas mixtures |
| FR2769656B1 (fr) | 1997-10-14 | 1999-12-17 | Air Liquide | Procede de realisation d'un paquet par assemblage d'une structure interieure de confinement de fluide, d'une structure exterieure et d'equipements, et procede de construction sur site utilisant un tel paquet |
| FR2797942B1 (fr) * | 1999-08-24 | 2001-11-09 | Air Liquide | Vaporiseur-condenseur et installation de distillation d'air correspondante |
| FR2806325B1 (fr) * | 2000-03-17 | 2002-10-18 | Air Liquide | Module de garnissage, son procede de fabrication, et appareil de traitement de fluide(s) comportant un garnissage correspondant |
| AU2003272218A1 (en) * | 2002-08-08 | 2004-02-25 | Pacific Consolidated Industries, L.P. | Nitrogen generator |
| FR2844040A1 (fr) * | 2002-08-28 | 2004-03-05 | Air Liquide | Echangeur de chaleur a plaques brasees et installation correspondante |
| GB0307404D0 (en) * | 2003-03-31 | 2003-05-07 | Air Prod & Chem | Apparatus for cryogenic air distillation |
| FR2880418B1 (fr) * | 2004-12-30 | 2007-04-27 | Air Liquide | Ensemble d'echangeurs de chaleur, appareil de distillation cryogenique incorporant un tel ensemble et procede de distillation cryogenique utilisant un tel ensemble |
| JP2006275462A (ja) * | 2005-03-30 | 2006-10-12 | Taiyo Nippon Sanso Corp | 窒素ガス製造装置 |
| DE102005022091A1 (de) * | 2005-05-12 | 2006-02-23 | Linde Ag | Verfahren zum Herstellen einer verfahrenstechnischen Anlage |
| CN101033910B (zh) * | 2007-04-12 | 2011-07-27 | 杭州杭氧股份有限公司 | 集成空气分离与液化天然气冷量回收系统 |
| CN101338965A (zh) * | 2008-01-31 | 2009-01-07 | 杭州福斯达气体设备有限公司 | 一种中型空分设备分馏塔冷箱组装方法 |
| EP2462291A1 (fr) * | 2009-08-07 | 2012-06-13 | Conocophillps Company | Moyen de fixation d'isolation cryogénique et procédé correspondant |
| DE102010012920A1 (de) * | 2010-03-26 | 2011-09-29 | Linde Aktiengesellschaft | Vorrichtung zur Tieftemperaturzerlegung von Luft |
| FR2962799B1 (fr) * | 2010-07-13 | 2014-07-04 | Air Liquide | Ensemble de refroidissement et appareil de separation d'air par distillation cryogenique comprenant un tel ensemble de refroidissement |
| KR101175139B1 (ko) * | 2011-01-17 | 2012-08-20 | 대한전기공업 주식회사 | 방향 전환 방식을 적용한 응축장치 |
| CN202133229U (zh) * | 2011-06-07 | 2012-02-01 | 上海启元气体发展有限公司 | 一种大型空气分离设备的冷箱 |
| DE102012008416A1 (de) * | 2012-04-27 | 2013-10-31 | Linde Aktiengesellschaft | Verrohrungsmodul für Luftzerlegungsanlage |
| PL2657633T3 (pl) * | 2012-04-27 | 2020-04-30 | Linde Aktiengesellschaft | Moduł orurowania do instalacji do rozdziału powietrza |
| DE102012008415A1 (de) * | 2012-04-27 | 2013-10-31 | Linde Aktiengesellschaft | Transportables Paket mit einer Coldbox, Tieftemperatur-Luftzerlegungsanlage und Verfahren zum Herstellen einer Tieftemperatur-Luftzerlegungsanlage |
| FR3017939B1 (fr) * | 2014-02-24 | 2019-03-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Appareil de separation par distillation cryogenique comprenant une pluralite d’elements modulaires |
| US20160245585A1 (en) * | 2015-02-24 | 2016-08-25 | Henry E. Howard | System and method for integrated air separation and liquefaction |
-
2016
- 2016-06-06 FR FR1655113A patent/FR3052244B1/fr not_active Expired - Fee Related
- 2016-06-06 FR FR1655111A patent/FR3052242B1/fr not_active Expired - Fee Related
- 2016-06-06 FR FR1655112A patent/FR3052243B1/fr not_active Expired - Fee Related
-
2017
- 2017-06-02 CN CN201780044326.6A patent/CN109564059B/zh not_active Expired - Fee Related
- 2017-06-02 CN CN201780035404.6A patent/CN109348726A/zh active Pending
- 2017-06-02 US US16/307,330 patent/US11215395B2/en not_active Expired - Fee Related
- 2017-06-02 WO PCT/FR2017/051384 patent/WO2017212145A1/fr not_active Ceased
- 2017-06-02 EP EP17733500.7A patent/EP3465036B1/fr active Active
- 2017-06-02 WO PCT/FR2017/051386 patent/WO2017212147A1/fr not_active Ceased
- 2017-06-02 EP EP17733503.1A patent/EP3465037B1/fr active Active
- 2017-06-02 US US16/307,655 patent/US20190301796A1/en not_active Abandoned
- 2017-06-02 WO PCT/FR2017/051383 patent/WO2017212144A1/fr not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| FR3052244A1 (fr) | 2017-12-08 |
| US20190137174A1 (en) | 2019-05-09 |
| WO2017212147A1 (fr) | 2017-12-14 |
| CN109564059B (zh) | 2021-06-29 |
| EP3465036B1 (fr) | 2020-09-16 |
| WO2017212144A1 (fr) | 2017-12-14 |
| EP3465037A1 (fr) | 2019-04-10 |
| CN109348726A (zh) | 2019-02-15 |
| FR3052242B1 (fr) | 2019-04-19 |
| EP3465037B1 (fr) | 2020-09-30 |
| FR3052242A1 (fr) | 2017-12-08 |
| US11215395B2 (en) | 2022-01-04 |
| FR3052244B1 (fr) | 2018-05-18 |
| WO2017212145A1 (fr) | 2017-12-14 |
| US20190301796A1 (en) | 2019-10-03 |
| CN109564059A (zh) | 2019-04-02 |
| FR3052243A1 (fr) | 2017-12-08 |
| FR3052243B1 (fr) | 2019-06-28 |
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