Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
  • B01D63/06—Tubular membrane modules
  • B01D63/066—Tubular membrane modules with a porous block having membrane coated passages
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/04—Tubular membranes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/10—Supported membranes; Membrane supports
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/10—Supported membranes; Membrane supports
  • B01D69/106—Membranes in the pores of a support, e.g. polymerized in the pores or voids

Definitions

• the present invention relates to a porous monolith support of a filter element having a tabular shape and a substantially constant cross-section along the direction of its axis and comprising a plurality of channels whose surfaces are intended to be coated by filtration membranes, these channels having cross sections distributed in the cross section of the support, all the channels being separated from the periphery of the support only by a single side wall of the support.
• a filter element comprises a porous monolithic support traversed by longitudinal channels whose lateral surface is coated with a filter membrane having a very small thickness and defining filtering mesh of determined size.
• a filter membrane having a very small thickness and defining filtering mesh of determined size.
• such a filter element allows the implementation in a liquid medium of a filtration process, microfiltration, ultrafiltration, nanofiltration or reverse osmosis.
• the fluid to be filtered circulates in the channels in the form of tangential currents in contact with the filtration membranes.
• the membranes ensure a separation of the circulating liquid medium at their contact by retaining certain particles or molecules and allowing other fractions of the liquid medium to pass through when they are subjected to a pressure established on either side of the membranes, called pressure transmembrane.
• the membranes being of very small thickness, they are of great fragility.
• the porous monolithic support provides the mechanical strength of the filter element so that membranes of very small thickness can be used.
• the channels are distributed in the section of the monolithic support in a particular arrangement.
• This arrangement as well as the size and the shape of the channels, are chosen according to various constraints, and in particular the viscosity of the fluid to be filtered, with the aim of maximizing the developed filtering surface, that is to say the membrane filter surface provided to the fluid for a reduced volume of the filter element, that is to say a reduced volume of the monolithic support.
• the hydraulic channel diameter defined by four times the cross-sectional area of a channel divided by its perimeter, must be large enough to allow a satisfactory flow of the fluid to be filtered in the channel, particularly in cases where the fluid to be filtered is viscous or loaded with suspended matter.
• a monolithic support having channels whose sections are formed by disk sectors distributed in a circle in a regular manner about its axis.
• the number of channels is commonly between three and six.
• the channels can be distributed over several concentric circumferences centered along the axis of the filter support.
• the permeate i.e., the fluid having passed through the membrane
• the permeate circulates inside the porous walls of the monolith support to move towards the outer surface of the support.
• the circulation conditions of the permeate are therefore very different depending on the position in the section of the filter element of the channel from which the permeate originates.
• the porous monolithic supports all channels of which are separated from the periphery of the support only by a single lateral wall of the support, are preferred.
• the channels consist of generally triangular sectors angularly offset (with rounded sharp angles) and distributed on the same circumference do not always lead to satisfactory performance when the diameter monolithic support is important, for example of the order of 25 mm. Indeed, if the number of channels is reduced, the developed filter surface may be small and if the number of channels is high, they are relatively flattened, so that the hydraulic diameter of the channels is reduced and may be insufficient for the circulation of certain viscous fluids.
• the purpose of the invention is to propose a porous monolith support whose geometry and the arrangement of the channels make it possible to optimize the developed membrane surface while preserving a sufficient hydraulic diameter, in particular for filtering viscous fluids or very charged suspensions, and provide high filtration performance even with monolithic carriers having a large outer diameter.
• the subject of the invention is a porous monolithic support of the aforementioned type, characterized in that all the channels of the support are distributed in:
• a second set of oblong lateral channels interposed between the radial channels and arranged with their length extending substantially parallel to the periphery of the support.
• the porous monolith support comprises one or more of the following characteristics:
• the number of radial channels and lateral channels is between 8 and 12; the length of the radial channels is greater than a quarter of the minimum transverse dimension of the support;
• the cross sectional area of the radial and lateral channels is between 18 and 30 mm 2 ; the width of the radial channels is between 0.3 and 0.6 times their length;
• the minimum transverse dimension of the support is between 24 mm and 30 mm, and the hydraulic diameter of each channel is between 4 and 6 mm;
• the radial channels have an elliptical section;
• the radial channels have a section in the form of a curvilinear triangle having a large convex side and two smaller concave sides;
• the lateral channels are arranged so that the large convex sides of their section extend substantially parallel to the periphery of the support;
• the radial channels have a polygonal shape with at least four sides, and the lateral channels have a generally triangular shape;
• the support comprises, for each pair of adjacent channels consisting of a radial channel and a lateral channel, a connecting passage ensuring communication between the associated radial and lateral channels; and - each connecting passage has a width less than half of the smallest length of the channels.
• the invention also relates to a filtration element comprising a porous monolith support delimiting a plurality of channels and filtration membranes coating the walls of the channels, characterized in that the porous monolith support is as defined above.
• the invention also relates to a fluid filtration module comprising a set of filtration elements according to that defined above.
• FIG. 1 is a fragmentary exploded perspective view of a module filtering apparatus comprising porous supports according to the invention
• FIG. 2 is a section of a porous monolith support according to the invention.
• FIGS. 5, 6 and 7 are views identical to those of FIGS. 2, 3 and 4 showing alternative embodiments of the respective monolithic supports of these figures; and - Figure 8 is a view identical to that of Figure 7 of yet another alternative embodiment.
• the filtration module 10 illustrated in FIG. 1 comprises a tubular body 12 in which are arranged parallel to each other filtration elements 13 formed of porous monolithic supports 14 according to the invention, the inner channels of which are covered with a porous membrane. 15. At each end, the porous monolithic supports are held by spacers 16 which are associated joints 18.
• the body 12 is extended at its ends by convergent sections 20, one of which forms an inlet for the fluid to be filtered and the other forms an outlet for collecting the retentate, that is to say the fluid that has not passed through the porous membranes.
• One or more lateral taps 22 are provided on the body 12 for collecting the permeate having passed through the porous membranes.
• the fluid to be filtered is conveyed inside the filtration channels.
• a pressure difference is established between the inner part of the channels carrying the membranes and the chamber formed outside the supports 14 and delimited by the body 12.
• a fraction of the fluid to be filtered passes through the filtration membranes and circulates through porous support 14 towards their outer surface.
• the monolithic support according to the invention is preferably made of porous ceramic material. It is formed in one piece, for example by a conventional method of extruding a ceramic material through a die of suitable shape forming the network of channel separation walls.
• FIG. 2 is shown a section of a porous monolith support 50 according to the invention.
• This has a cylindrical tabular shape of X-X axis of circular section.
• the diameter of the support is preferably between 20 mm and 30 mm and is, for example, equal to 25 mm.
• the section of the support 50 is constant along its length. This length can be in particular between 1000 and 1300 mm; it is for example equal to 1178 mm.
• the support 50 is traversed, along its entire length in the direction of the axis XX, by channels whose hydraulic diameter is generally between 4 and 6 mm, for example between 4.5 and 5.5 mm, their number being preferably between 8 and 12.
• the channels are separated from each other by partitions generally designated by the reference 54.
• the channels define with the outer cylindrical lateral surface of the support peripheral walls 56.
• All channels are separated from the periphery of the support only by a single side wall 56.
• the fluid flowing in each channel can reach the outer surface of the support while circulating only radially through a side wall, without having to borrow an intermediate partition 54.
• All channels of the support have a section of oblong shape, that is to say that this section is generally elongated and therefore has a length greater than its width. All the channels are distributed in a first set of radial channels 62 arranged with their length extending radially and a second set of lateral channels 64 interposed between the radial channels at the periphery of the support and arranged with their length extending generally parallel to the periphery of the support.
• no channel is arranged along the X-X axis.
• the radial channels 62 are angularly distributed regularly around the X-X axis.
• Their number is preferably between four and six. In the example, it is five, so that the lengths of the channel sections are angularly offset by 72 °.
• the lateral channels 64 are interposed between the radial channels 62.
• each lateral channel 64 is centered on a bisector of the angle defined by the lengths of the sections of the radial channels 62.
• the lengths of the lateral channels 64 extend along the sides a pentagon centered along the XX axis.
• the channels all have the same section.
• the cross sectional area of the channels is preferably between 18 mm 2 and 30 mm 2 . It is here of 23 mm 2 .
• the channel section is ellipsoidal in shape.
• the major axis of the ellipse has a length greater than half the radius of the support 50. Preferably, this length is substantially equal to two-thirds of the radius of the support.
• the length of the minor axis of the ellipse that is to say the width of the channel, is between one-third and two-thirds of the length of the major axis. Preferably, this is equal to substantially half the length of the major axis.
• the radial channels have a width of between 0.3 and 0.6 times their length.
• the minimum thickness of the side walls 56 is equal to 1.5 mm while the minimum thickness of the partitions 56 between the adjacent channels is equal to 0.8 mm.
• a support whose diameter here is equal to 25 mm and the length is here equal to
• FIG. 3 shows an alternative embodiment of the support of FIG. 2.
• the partitions and the side walls are designated by the same references 54 and 56.
• the support noted 70 is of cylindrical shape with a diameter of 25 mm. It defines five radial channels 72 between which are interspersed along the outer lateral surface five longitudinal channels 74.
• the channel section has a curvilinear triangle shape having a large convex side 76 and two smaller and concave small sides 78.
• the sides 78 have identical lengths.
• the sides defining the channels are connected to each other by filleting.
• the large convex side 76 extends substantially parallel to the cylindrical outer surface of the support.
• the radius of curvature of this large side 76 is equal to 22 mm and the center extends along the X-X axis of the support.
• the long sides 76 extend in the extension of each other and thus have the same circular envelope.
• each duct has a cross section with a perimeter of 20.5 mm and a surface area of 23.5 mm.
• the length of the channel sections here is about 8.8 mm.
• the radial channels extend with their length generally disposed from the center to the periphery. This length extends substantially radially, being slightly inclined, the latter delimiting with a diameter of the support an angle of twenty degrees. All the radial channels 72 are inclined relative to the associated diameter on the same side to the image of the blades of a helix. They are arranged in the same direction and are regularly angularly distributed so that the pattern defined by the channels is rotationally invariant about the axis of the support at an angle of 72 °.
• the minimum thickness of the side walls 56 separating the long sides 76 of the lateral channels of the outer surface of the support is equal to 1.5 mm, whereas the minimum thickness of the partitions 34 separating the radial channels of the longitudinal channels is equal to 1.2 mm.
• no channel is arranged along the X-X axis.
• the partitions 54 delimited between the different channels have a general shape of Y.
• the filtering surface of such a support with a diameter of 28.8 mm and a length of 1178 mm is equal to 0.240 m 2 for a hydraulic diameter of 4.65 mm.
• the radial channels denoted 92 and the lateral channels denoted 94 have different shapes.
• the radial channels 92 extend with their length arranged exactly radially. These channels, five in number, are angularly offset by 72 °. They have in section a polygonal shape with more than four sides, this number being in particular equal to five, so that these channels have an irregular pentagon shape.
• the section of the radial channels is symmetrical with respect to the length of the channels. They present from the center of the support two small sides 96.
• each radial channel 92 has a narrow bottom-forming side 98 extending generally parallel to the outer surface of the support. This bottom is connected to the ends of the short sides two long sides 100.
• the length of the radial channels 92 is here substantially equal to 9.3 mm while their width, measured between the points connecting the short sides 96 to the long sides 100, is equal to 4.1 mm.
• the longitudinal channels 94 have in section a curvilinear triangle shape having a curved base 102 extending generally parallel to the lateral surface of the support and two straight sides 104 of the same length extending parallel to the long sides 100 of the two radial channels between which the longitudinal channel is inserted.
• the base 102 has a longer length than the straight sides 104.
• the length of the side channels is 7.8 mm while their width is 5 mm.
• the partitions 54 delimited between the adjacent radial channels 92 and the lateral channel 94 interposed have a general shape of Y, the thickness of the partitions being constant along each branch of the Y and for example substantially equal to 1.2 mm.
• no channel is arranged along the X-X axis.
• the thickness of the walls 56 separating the channels from the outer surface is equal to 1.8 mm. In all channels, the successive sides delimiting the channels connect to each other by connecting fillet or rounded sharp angles.
• the porous support having a diameter of 25 mm for a length of 1178 mm, offers an expanded filtering surface of 0.245 m 2 , the hydraulic diameter of the radial channels 92 being equal to 4.83 mm whereas is 4.81 mm for the side channels 94.
• porous supports illustrated in FIGS. 2, 3 and 4 comprise channels which are disjoint from one another.
• the radial channels are totally separated from the side channels by continuous partitions.
• a connecting passage connects two by two an adjacent radial channel and an adjacent lateral channel in order to ensure fluidic communication between these channels.
• This connecting passage is relatively short and in particular preferably has a width less than half and preferably one third of the smaller length of the radial and lateral channels.
• FIGS. 5 to 8 the different elements of the supports corresponding to those of FIGS. 2 to 4 are designated by the same reference numerals.
• the radial channels 62 and the side channels 64 are connected to each other from their point by a connecting passage 120 located in the vicinity of the periphery of the support.
• each pair of radial and lateral channels thus connected defines in section a general V shape.
• the adjacent radial and side channels are connected to each other from their corner nearest the periphery of the support by a passage 130.
• This connection is provided between two adjacent channels through an intermediate partition 54 defined by two small concave sides 78 arranged facing one another.
• the channels 92 and 94 are connected to each other by a connecting passage 140 formed through the partition 54 delimited between a large side
• the passage noted 140 is formed in the half of the partition extending on the side of the periphery of the support.
• the passage marked 150 is delimited through the same partition in its half disposed away from the periphery of the porous monolithic support 50.
• the monolithic supports have a polygonal outer section, in particular hexagonal or square.
• the dimensional relationships mentioned in the description apply by replacing the diameter of the support by the minimum transverse dimension of its section.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Separation Using Semi-Permeable Membranes (AREA)

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• 2004
  • 2004-10-27 FR FR0411471A patent/FR2876922B1/fr not_active Expired - Fee Related
• 2005
  • 2005-10-21 WO PCT/FR2005/002622 patent/WO2006045933A1/fr active Application Filing
  • 2005-10-21 US US11/577,496 patent/US20080296217A1/en not_active Abandoned
  • 2005-10-21 EP EP05812416A patent/EP1835984A1/de not_active Withdrawn
  • 2005-10-21 CN CNA2005800369015A patent/CN101048220A/zh active Pending

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