• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Membrane separation device comprising a tubular membrane or a cylindrical set of hollow fiber membranes bounded by a tubular casing (1) connecting two caps (2) pierced with through holes (3) held together with said casing by two systems of tightening and sealing, characterized in that: - each clamping and sealing system is a clamping collar (4) provided with an integrated seal having two independent half-parts interconnected in service position by means of at least one screw (5) or a clamping bolt - the tubular casing (1) has a diameter d and at each end a groove (6) adapted to receive an edge of the clamp (4) of one of the two clamping and sealing systems, and - each cap (2) is composed of a curved bottom and a cylindrical portion having a diameter D such that D <d and a groove (7) adapted to receive an edge of clamp 4 of one of the two clamping and sealing systems.
    公开号:FR3077508A1
    申请号:FR1850964
    申请日:2018-02-06
    公开日:2019-08-09
    发明作者:Thierry Roussel
    申请人:Air Liquide SA；LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude；
    IPC主号:
    专利说明:

    The present invention relates to a membrane separation device and to a module comprising several of these devices.
    It relates in particular to the purification of biogas, with the aim of producing biomethane in accordance with the specifications for injection into a natural gas network.
    Biogas is the gas produced during the degradation of organic matter in the absence of oxygen (anaerobic fermentation) also called methanization. It can be a natural degradation - we observe it in marshes or household waste dumps, but the production of biogas can also result from the methanisation of waste in a dedicated reactor, called methanizer or digester.
    Due to its main constituents - methane and carbon dioxide - biogas is a powerful greenhouse gas; it also constitutes, at the same time, an appreciable source of renewable energy in a context of scarcity of fossil fuels.
    Biogas mainly contains methane (CH4) and carbon dioxide (CO2) in variable proportions depending on the method of production, but also, in smaller proportions, water, nitrogen, hydrogen sulfide, oxygen, as well as other organic compounds, in trace amounts.
    Depending on the degraded organic matter and the techniques used, the proportions of the components differ, but on average biogas comprises, on dry gas, from 30 to 75% of methane, from 15 to 60% of CO2, from 0 to 15% of nitrogen, 0 to 5% oxygen and trace compounds.
    Biogas is valued in different ways. After a light treatment, it can be used near the production site to provide heat, electricity or a mixture of the two (cogeneration); the high content of carbon dioxide reduces its calorific value, increases the compression and transport costs and limits the economic interest of its recovery to this local use.
    Further purification of the biogas allows its wider use, in particular, further purification of the biogas makes it possible to obtain a biogas purified to the specifications of natural gas and which may be substituted for it; the biogas thus purified is “biomethane”. Biomethane thus complements natural gas resources with a renewable part produced in the heart of the regions; it can be used for exactly the same uses as natural gas of fossil origin. It can supply a natural gas network, a filling station for vehicles, it can also be liquefied to be stored in the form of liquid natural gas (LNG) ...
    The methods of valorization of biomethane are determined according to the local contexts: local energy needs, possibilities of valorization as biomethane fuel, existence close to networks of distribution or transport of natural gas in particular. Creating synergies between the various actors working on a territory (farmers, industrialists, public authorities), the production of biomethane helps the territories to acquire greater energy autonomy.
    Several steps must be taken between the collection of biogas and the obtaining of biomethane, the final product capable of being compressed or liquefied.
    In particular, several steps are necessary before the treatment which aims to separate the carbon dioxide to produce a stream of purified methane. A first step consists in compressing the biogas which has been produced and conveyed at atmospheric pressure, this compression can be obtained - conventionally - via a lubricated screw compressor. The following stages aim to rid the biogas of the corrosive components that are hydrogen sulphide and volatile organic compounds (VOCs), the technologies used are conventionally pressure-modulated adsorption (PSA) and trapping on activated carbon. Then comes the step which consists in separating the carbon dioxide in order to have methane in fine at the purity required for its subsequent use.
    Carbon dioxide is a contaminant typically found in natural gas which it is common to have to remove. Various technologies are used for this depending on the situation; among these, membrane technology is particularly effective when the CO2 content is high; it is therefore particularly effective in separating the CO2 present in biogas, and in particular in landfill gas.
    The membrane gas separation processes used for the purification of a gas, whether they use one or more stages of membranes, must allow the production of a gas of the required quality, at a low cost, while minimizing the losses of the gas that we want to develop. Thus, in the case of the purification of biogas, the separation carried out is mainly a CH4 / CO2 separation, which should allow the production of a gas containing, depending on its use, more than 85% of CH4, preferably more than 95% of CH4, more preferably more than 97.5% of CH4, while minimizing the losses of CH4 in the waste gas and the cost of purification, the latter being for a large part linked to the electrical consumption of the gas compression device upstream of the membranes.
    To perform this membrane separation, two types of membranes are mainly known: tubular membranes and hollow fiber membranes.
    Tubular membranes can be single-channel or multi-channel and are often mineral in nature. In the case of multi-channel tubular membranes, the tubes are grouped in parallel in a module. The permeate is recovered outside the tubes, in the envelope of the module.
    Hollow fiber membranes are composed of a set of hollow fibers grouped in an envelope (forming the module). They are only organic in nature and do not have a textile support (self-supporting). Likewise, they are often made of only one material, although composite hollow fibers exist. The active layer (skin) and the porous sub-layer are intimately connected, which makes it possible to filter in both directions.
    Until now, the envelope of the membrane consists of a cylindrical tube A with a diameter greater than that of the membrane (Figure 1). This tube has an opening consisting of a welded sleeve allowing the outlet D of the permeate gas from the envelope.
    At each end of the tube are welded two sets of tubes - flanges B drilled around their periphery of tapped blind holes.
    These tube-flange B assemblies have an internal diameter as close as possible to that of the membrane in order to ensure sealing between the gas inlet / outlet and the permeate outlet D of the membrane. This seal is ensured by an O-ring placed in a groove C machined at each end of the membrane.
    On each flange, two flat bottoms F pierced on their outside diameter with through threaded holes, equivalent in number and in position to those of the flanges, close the envelope.
    These flat bottoms F have in their center an opening consisting of a welded sleeve G allowing the entry / exit of the gas in the envelope.
    The flat bottom is clamped on the flange using a screw-washer assembly H passing through the corresponding threaded holes in the flat bottoms and flanges.
    The seal is ensured by an O-ring placed in a groove E, machined on each flat bottom, which comes to crash against the flange during tightening.
    The envelope is supported by 4 metallic I-shaped pieces welded to the envelope (in diametrically opposite pairs), which can be screwed onto a support and thus allowing a variable number of membranes to be mounted on a module J others.
    However, the main disadvantages of this type of envelope are:
    - To ensure the assembly / disassembly of the membranes, it is necessary to compensate for the manufacturing tolerances and deformations due to the welds by precisely re-machining the inside diameter of the tube-flange assemblies after manufacture and welding with the tube. However even after re-machining the assembly / disassembly of the membranes remains very difficult.
    - The positioning of the envelopes on the module, which is very constrained by the welded L-shaped support pieces, can cause problems.
    - Removing a membrane from its envelope requires unscrewing the two flat bottoms, then manually pushing the membrane out of its envelope. Long and very difficult operation due to the number of screws and the friction forces involved.
    From there, a problem is to provide an improved membrane separation device.
    A solution of the present invention is a membrane separation device comprising a tubular membrane or a cylindrical assembly of hollow fiber membranes limited by a tubular casing 1 connecting two caps 2 pierced with through holes 3 held jointly with said casing by two clamping and sealing systems, characterized in that:
    - each clamping and sealing system is a clamp 4 provided with an integrated seal having two independent half-parts connected together in the service position by means of at least one screw 5 or a clamping bolt
    the tubular casing 1 has a diameter d and at each end a groove 6 capable of receiving an edge of the clamping collar 4 of one of the two clamping and sealing systems, and
    - Each cap 2 is composed of a curved bottom and a cylindrical part having a diameter D such that D <d and a groove 7 capable of receiving an edge of the clamp 4 of one of the two clamping systems and d sealing.
    Preferably X <D with X chosen so as to ensure the seal between the tubular casing and the cap.
    The tightening and sealing between the caps and the tubular casing is ensured by the VICTAULIC type collar technology: a circular joint of practically the width of the collar is positioned either on the cap or on the tubular casing, the cap and the tube are approached from each other, then the seal is positioned astride the cap and the tube. The collar is then closed on the joint and the assembly is positioned so that the edges of the collar are placed in the grooves provided for this purpose, one machined on the outside of the cap and the other on the outside. of the tube. Finally, the clamping of the collar is carried out using the two screws at its ends, the seal thus crushed comes to seal between the two elements.
    Depending on the case, the membrane separation device can have one or more of the following characteristics:
    - the through holes 3 of the drilled caps 2 each comprising a threaded sleeve (8) so as to allow the introduction of a disassembly tool 9;
    - The clamp comprises two screws making it possible to connect two independent half-parts together;
    - The cylindrical part of the caps have a height of between 20 mm and 60 mm. Preferably this height is between the thickness of the O-ring placed in the machined groove of and this same thickness of seal plus the difference in length between the longest tubular casing and the shortest tubular casing that is wish to install halved;
    - The cylindrical part of the cap 2 has a diameter D of between 100 and 400 mm;
    - The tubular casing 1 has a diameter d between 100 and 400 mm;
    - The tubular casing 1 has a length of between 780 and 830 mm;
    - Each of the grooves 6 of the tubular casing 1 is located at a distance between 12 and 25 mm from the end of the casing which is closest to it;
    - The groove 7 of each cap 2 is located at a distance between 12 and 25 mm from the end of said cap;
    As examples, the device may have the following characteristics:
    - diameter D of the cap - 152.35 mm + or - 0.1 mm,
    - diameter d of the tubular casing - 159.2 mm,
    - height of the cylindrical part of the cap - M mm,
    - distance between the grooves of the tubular casing and the ends closest to the tubular casing - 16.60 mm + or -0.76 mm,
    - distance between the grooves of the caps and the ends of the caps: 16.60 mm + or -0.76 mm; and
    - length of the tubular casing - 812 mm.
    or the following characteristics:
    - diameter D of the cap - 301.7 mm + or - 0.1 mm,
    - diameter d of the tubular casing - 309.68 mm,
    - height of the cylindrical part of the cap - 40 mm,
    - distance between the grooves of the tubular casing and the ends closest to the tubular casing - 19.05 mm + or -0.76 mm,
    - distance between the grooves of the caps and the ends of the caps: 19.05 mm + or -0.76 mm; and
    - length of the tubular casing - 800 mm.
    The present invention also relates to a membrane separation module comprising:
    - at least two membrane separation devices according to the invention,
    - a support, and
    - At least two pairs of metal parts 10 screwed to the support and having a cradle shape, each pair of metal parts receiving a membrane separation device. Preferably, said module comprises at least one retaining collar (11) per membrane separation device making it possible to maintain said membrane separation device on the pair of metal parts.
    Each retaining collar will preferably be screwed to the support.
    In the context of the present invention, the tubular casing is placed on two metal parts in cradles which can be screwed onto a support and thus allowing a module to mount a variable number of membranes one next to the other. Once the membrane in position, two commercial necklaces independent of the metal parts and screwing onto the same support as the metal parts keep the envelope in position. Note that there are no welding constraints between the tubular casing and the metal parts since the tubular casing is only placed on the metal parts in cradles.
    The advantages of the device and of the membrane separation module according to the invention are the following:
    - The assembly / disassembly of the membrane is facilitated by the flexibility of the cap-tubular envelope connection which allows the cap to be positioned so as to easily recover manufacturing tolerances.
    - The weight of a body is reduced significantly which makes it easy to assemble and transport.
    -The support of the envelope on the metal parts in cradles and the maintenance by independent collars allows a non-restrictive positioning and further facilitates the installation of the membranes on a support such as a module.
    - Removing a membrane from its envelope is much simpler and much shorter thanks to the use of tools:
    On the side where you want the membrane to come out, you can easily extract the bottom using the VICTAULIC collar, no screws / studs to dismantle.
    On the side opposite to that where you want to extract the membrane, you simply screw the mounting tool into the threaded sleeve using a key, it will push the membrane until it is extracted.
    -The risks of gas leaks to the outside of the membrane envelope are reduced due to the disappearance of the groove-O-ring assembly.
    The membrane separation module according to the invention will preferably be used for the production of methane from biogas.
    权利要求:
    Claims (13)
    [1" id="c-fr-0001]
    claims
    1. Membrane separation device comprising a tubular membrane or a cylindrical assembly of hollow fiber membranes limited by a tubular casing (1) connecting two caps (2) pierced with through holes (3) held together with said casing by two clamping and sealing systems, characterized in that:
    - each clamping and sealing system is a clamping collar (4) provided with an integrated seal having two independent half-parts connected together in the operating position by means of at least one screw (5) or a bolt Clamping
    the tubular casing (1) has a diameter d and at each end a groove (6) capable of receiving an edge of the clamping collar (4) of one of the two clamping and sealing systems, and
    - Each cap (2) is composed of a curved bottom and a cylindrical part having a diameter D such that D <d and a groove (7) capable of receiving an edge of the clamp 4 of one of the two systems tightening and sealing.
    [2" id="c-fr-0002]
    2. Device according to claim 1, characterized in that the through holes (3) of the caps (2) drilled each comprising a threaded sleeve (8) so as to allow the introduction of a disassembly tool (9).
    [3" id="c-fr-0003]
    3. Device according to one of claims 1 or 2, characterized in that the clamp comprises two screws for connecting together two independent half-parts.
    [4" id="c-fr-0004]
    4. Device according to one of claims 1 to 3, characterized in that the cylindrical part of the caps have a height between 20 mm and 60 mm.
    [5" id="c-fr-0005]
    5. Device according to one of claims 1 to 4, characterized in that the cylindrical part of the cap (2) has a diameter D between 100 and 400 mm.
    [6" id="c-fr-0006]
    6. Device according to one of claims 1 to 5, characterized in that the tubular casing (1) has a diameter d between 100 and 400 mm.
    [7" id="c-fr-0007]
    7. Device according to one of claims 1 to 6, characterized in that the tubular casing (1) has a length between 780 and 830 mm.
    [8" id="c-fr-0008]
    8. Device according to one of claims 1 to 7, characterized in that each of the grooves (6) of the tubular casing (1) is located at a distance between 12 and 25 mm from the end of the casing who is closest to him.
    [9" id="c-fr-0009]
    9. Device according to one of claims 1 to 8, characterized in that the groove (7) of each cap (2) is located at a distance between 12 and 25 mm from the end of said cap.
    [10" id="c-fr-0010]
    10. Membrane separation module comprising:
    - at least two membrane separation devices according to one of claims 1 to 9,
    - a support, and
    - At least two pairs of metal parts (10) screwed to the support and having a cradle shape, each pair of metal parts receiving a membrane separation device.
    [11" id="c-fr-0011]
    11. Module according to claim 10, characterized in that said module comprises at least one retaining collar (11) per membrane separation device making it possible to maintain said membrane separation device on the pair of metal parts.
    [12" id="c-fr-0012]
    12. Module according to claim 11, characterized in that each retaining collar is screwed to the support.
    [13" id="c-fr-0013]
    13. Use of a membrane separation module according to one of claims 10 to 12 for the production of methane from biogas.
    类似技术:
    公开号 | 公开日 | 专利标题
    EP1890961B1|2017-02-22|Method for simultaneously producing hydrogen and carbon monoxide
    EP3520884A1|2019-08-07|Device for separating membranes
    EP3046655B1|2019-11-06|Method and apparatus for the final purification of biogas for producing biomethane
    EP3369473A1|2018-09-05|Facility and method for treatment of a feed gas stream comprising methane and carbon dioxide by membrane permeation
    FR2916363A1|2008-11-28|PROCESS FOR PURIFYING A CPSA GAS WITH TWO REGENERATION BEARINGS AND PURIFICATION UNIT FOR CARRYING OUT SAID METHOD
    EP3666368A1|2020-06-17|System and method for treating a gaseous current by membrane permeation with adjustment of the methane concentration
    EP3666367A1|2020-06-17|System and method for treating a gaseous current by membrane permeation with adjustment of the suction pressure of the second permeate
    FR2904821A1|2008-02-15|PROCESS FOR PURIFYING HYDROGEN
    EP3613493A1|2020-02-26|Treatment by membrane permeation with adjustment of the number of membranes implemented according to the pressure of the feed gas stream
    FR3025117A1|2016-03-04|PROCESS FOR PURIFYING BIOGAS BY MEMBRANE | AT NEGATIVE TEMPERATURE
    WO2019122660A1|2019-06-27|Cryogenic process for removing nitrogen from a discharge gas
    EP3666369A1|2020-06-17|System and method for treating a gaseous current by membrane permeation with adjustment of the suction pressure of the third permeate
    EP3666880B1|2021-04-14|Combined method for anaerobic digestion and methanation
    FR2969136A1|2012-06-22|Producing carbon monoxide combined with production of hydrogen from hydrocarbon mixture, by reforming hydrocarbon mixture to obtain synthesis gas, cooling synthesis gas with heat recovery, and extracting carbon dioxide in cooled syngas
    EP3610940A1|2020-02-19|Treatment by membrane permeation with adjustment of the temperature of the first retentate according to the ch4 concentration in the third and/or fourth permeate
    EP3628389A1|2020-04-01|Method for producing biomethane from a flow of biogas comprising solidification of impurities
    EP3756750A1|2020-12-30|Installation for the treatment of a flow of methane and carbon dioxide by means of a vane compressor and a membrane separator unit
    EP3610939A1|2020-02-19|Treatment by membrane permeation with adjustment of the pressure of the feed gas stream according to the ch4 concentration in the second retentate
    EP3142967B1|2019-02-20|Treatment method for separating carbon dioxide and hydrogen from a mixture
    EP3892357A1|2021-10-13|System for treating biogas by membrane permeation with adaptation of the membrane surface according to the pressure of biogas
    WO2021228616A1|2021-11-18|Facility and method for producing biomethane with limited methane loss and limited co2 emissions
    FR3075660B1|2019-11-15|PROCESS FOR DISTILLING A GASEOUS CURRENT CONTAINING OXYGEN
    WO2020079337A1|2020-04-23|Installation and method for producing liquefied methane
    FR3112767A1|2022-01-28|Optimized production of hydrogen from a hydrocarbon.
    同族专利:
    公开号 | 公开日
    EP3520884A1|2019-08-07|
    FR3077508B1|2020-06-05|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US20020074277A1|2000-11-24|2002-06-20|Membrane Concepts, S.L.|Filter assembly, system and method for filtering fluids|
    WO2014198501A1|2013-06-12|2014-12-18|Evonik Fibres Gmbh|Membrane cartridge system|
    WO2016143920A1|2015-03-09|2016-09-15|주식회사 세프라텍|Separation membrane contactor module and membrane contact system and membrane contact method for purifying bio-gas using same|
    WO2017105356A1|2015-12-18|2017-06-22|Ak-Kim Kimya Sanayi Ve Ticaret Anonim Sirketi|Hollow fiber membrane module|
    CN110917886A|2019-11-20|2020-03-27|湖南欧威爱特新材料科技有限公司|Tubular milipore filter packaging hardware|
    CN112354369A|2020-11-12|2021-02-12|湖南欧威爱特新材料科技有限公司|Packaging hardware is used in production of nanometer milipore filter convenient to it is fixed|
    法律状态:
    2019-02-20| PLFP| Fee payment|Year of fee payment: 2 |
    2019-08-09| PLSC| Publication of the preliminary search report|Effective date: 20190809 |
    2020-02-19| PLFP| Fee payment|Year of fee payment: 3 |
    2021-02-24| PLFP| Fee payment|Year of fee payment: 4 |
    2022-02-16| PLFP| Fee payment|Year of fee payment: 5 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1850964|2018-02-06|
    FR1850964A|FR3077508B1|2018-02-06|2018-02-06|MEMBRANE SEPARATION DEVICE|FR1850964A| FR3077508B1|2018-02-06|2018-02-06|MEMBRANE SEPARATION DEVICE|
    EP19155135.7A| EP3520884A1|2018-02-06|2019-02-01|Device for separating membranes|
    [返回顶部]