Patent Application
20170232403
The present invention relates to a filtration module and a filtration apparatus.
Filtration apparatuses equipped with filtration modules that include bundles of hollow fiber membranes have been used as solid liquid separation treatment apparatuses in wastewater treatment, processes of producing medicines, and the like. Examples of the filtration modules include external pressure modules in which the pressure on the outer circumferential side of the hollow fiber membranes is increased so that the feed liquid will penetrate into the inner circumferential side of the hollow fiber membranes, immersion type modules in which the feed liquid is caused to permeate into the inner circumferential side by osmotic pressure or by decreasing the pressure at the inner circumferential side, and internal pressure modules in which the pressure at the inner circumferential side of the hollow fiber membranes is increased so that the feed liquid will permeate toward the outer circumferential side of the hollow fiber membranes.
Of the filtration modules described above, the external pressure type and immersion type filtration modules become contaminated as substances contained in the feed liquid adhere to the surfaces of the hollow fiber membranes due to operation and their filtration ability will be degraded if left contaminated.
To address this issue, a cleaning method (air scrubbing) has been employed with which air bubbles are supplied from below the filtration modules so that the air bubbles abrade the surfaces of the hollow fiber membranes and vibrate the hollow fiber membranes to remove the adhering substances (refer to Japanese Unexamined Patent Application Publication No. 2010-42329).
PTL 1: Japanese Unexamined Patent Application Publication No. 2010-42329
In general, air bubbles for cleaning the surfaces of the hollow fiber membranes are continuously supplied to keep the surfaces of the hollow fiber membranes clean. Thus, if the cleaning efficiency at which the surfaces of the hollow fiber membranes are cleaned by air bubbles is degraded, the energy needed to supply air bubbles for cleaning may increase and the filtration cost may rise.
To reduce the filtration cost, an approach has been taken in which multiple filtration modules are connected in a vertical direction. However, air bubbles may diffuse due to holding members (the components that join the filtration modules) that hold the hollow fiber membranes, the surfaces of the hollow fiber membranes in the upper part may not come into contact with air bubbles, and the cleaning ability may be degraded as a result.
The present invention has been made under these circumstances and aims to provide a filtration module and a filtration apparatus that have excellent hollow fiber membrane surface cleaning efficiency and excellent filtration ability.
A filtration module according to an embodiment of the present invention made to solve the problem described above includes a plurality of hollow fiber membranes held while being aligned in one direction and a pair of holding members that fix both ends of the hollow fiber membranes. In the holding members, an existence region where the hollow fiber membranes exist has a rectangular shape in a direction perpendicular to the direction in which the hollow fiber membranes are aligned; a ratio of an average length of the existence region in a long side direction to an average length of the existence region in a short side direction is 10 or more and 50 or less; an average outer diameter of the hollow fiber membranes is 1 mm or more and 6 mm or less; and a ratio of an average effective length of the hollow fiber membranes between the holding members to the average length of the existence region in the short side direction is 40 or more and 200 or less.
The filtration module according to an embodiment of the present invention has excellent hollow fiber membrane surface cleaning effect and excellent filtration ability.
1 filtration module
2 hollow fiber membrane
2
a support layer
2
b filtration layer
3 upper holding member
3
a hollow casing
3
b resin composition
4 lower holding member
11 filtration vessel
12 air bubble supply unit
13 discharge duct
14 suction pump
[Description of Embodiments of the Present Invention]
A filtration module according to an embodiment of the present invention includes a plurality of hollow fiber membranes held by being aligned in one direction and a pair of holding members that fix both ends of the hollow fiber membranes. In the holding members, an existence region where the hollow fiber membranes exist has a rectangular shape in a direction perpendicular to the direction in which the hollow fiber membranes are aligned. The ratio of an average length of the existence region in a long side direction to an average length of the existence region in a short side direction is 10 or more and 50 or less. The average outer diameter of the hollow fiber membranes is 1 mm or more and 6 mm or less. The ratio of an average effective length of the hollow fiber membranes between the holding members to the average length of the existence region in the short side direction is 40 or more and 200 or less.
In the existence region in a direction perpendicular to the alignment direction where the hollow fiber membranes exist, because the ratio of the average length in the long side direction to the average length in the short side direction is within the above-described range, the filtration module can securely obtain a total number of hollow fiber membranes and a filtration area needed while keeping the length in the short side direction small. Furthermore, according to this filtration module, because the length in the short side direction of the existence region is small, the bundle of the hollow fiber membranes extending from the existence region has a smaller thickness in the short side direction and thus air bubbles easily reach inside the bundle of the hollow fiber membranes. Moreover, in the filtration module, because the length in the short side direction of the existence region is decreased, the hollow fiber membranes can bend in such a way as to increase the thickness of the hollow fiber membrane bundle in the short side direction, thereby facilitating titubation of the hollow fiber membranes. Moreover, according to the filtration module, because the average outer diameter of the hollow fiber membranes is within the above-described range, the hollow fiber membranes have sufficient strength and flexibility and the scrubbing effect can be enhanced since the hollow fiber membranes have strength that withstands air scrubbing and vibrate while being bent in the direction perpendicular to the alignment direction as a result of air scrubbing. According to the filtration module, because the ratio of the average effective length of the hollow fiber membranes between the holding members to the average length of the existence region in the short side direction is within the above-described range, the hollow fiber membranes undergo sufficient titubation due to abrasion with air bubbles, thereby forming gaps between the hollow fiber membranes through which air bubbles penetrate, and the cleaning effect is enhanced since this helps supply air bubbles to the hollow fiber membranes located on the inner side of the existence region. As such, the filtration module has excellent hollow fiber membrane surface cleaning efficiency and excellent filtration ability.
The packing area ratio of the hollow fiber membranes in the existence region is preferably 20% or more and 60% or less. When the packing area ratio of the hollow fiber membranes in the existence region is within this range, the filtration flow rate per facility area can be increased while reliably obtaining the cleaning effect on the inner side of the existence region.
The hollow fiber membranes are preferably arranged into a matrix in the long side direction and the short side direction of the existence region and, in the existence region, the average pitch of the hollow fiber membranes in the long side direction is preferably larger than the average pitch in the short side direction. When the average pitch of the hollow fiber membranes in the long side direction is larger than the average pitch in the short side direction as such, gaps that allow penetration of air bubbles are easily formed between the hollow fiber membranes in the short side direction due to titubation of the hollow fiber membranes and thus penetration of the air bubbles into the inner side of the existence region can be promoted.
The ratio of the average pitch in the short side direction to the average outer diameter of the hollow fiber membranes is preferably 1 or more and 1.5 or less. When the ratio of the average pitch in the short side direction to the average outer diameter of the hollow fiber membranes is within the above-described range, the filtration area can be increased by increasing the density of the hollow fiber membranes in the short side direction while maintaining the efficiency of forming gaps through which air bubbles can penetrate in the short side direction. Thus, the filtration flow rate per facility area can be increased.
The average effective length of the hollow fiber membranes between the holding members is preferably 1 m or more and 6 m or less. When the average effective length of the hollow fiber membranes is within this range, the hollow fiber membranes bend easily to promote formation of gaps that guide air bubbles to the inner side of the existence region, and breaking of the hollow fiber membranes due to vibration and the like can be prevented.
The hollow fiber membranes may each include a support layer containing polytetrafluoroethylene as a main component and a filtration layer stacked on a surface of the support layer and containing polytetrafluoroethylene as a main component.
Because the hollow fiber membranes have a support layer and a filtration layer both containing polytetrafluoroethylene as a main component, the hollow fiber membranes have sufficient mechanical strength.
The filtration layer is preferably formed by wrapping a stretched polytetrafluoroethylene sheet around a stretched polytetrafluoroethylene tube that constitutes a support layer and performing sintering. Because the hollow fiber membranes are formed by wrapping an stretched polytetrafluoroethylene sheet around an stretched polytetrafluoroethylene tube that constitutes a support layer and performing sintering, adjustment of the shape and size of the pores in the hollow fiber membranes is facilitated and pores in the support layer and the filtration layer become connected to one another to improve permeability.
At least one of the pair of holding members preferably include a hollow casing into which ends of the hollow fiber membranes are inserted and a resin composition containing an epoxy resin or a urethane resin as a main component preferably fill the space between an inner side wall surface of the hollow casing and outer circumferential surfaces of the hollow fiber membranes. When a resin composition containing an epoxy resin or a urethane resin as a main component fills the space between an inner side wall surface of the hollow casing and outer circumferential surfaces of the hollow fiber membranes as such, the gaps between the hollow casing and the hollow fiber membranes can be sealed, the outer side and the inner side of the hollow fiber membranes can be assuredly isolated from each other, and the hollow fiber membranes can be held and prevented from falling even when large vibrations occur by contact with air bubbles.
A filtration apparatus according to an embodiment of the present invention includes the filtration module, a filtration layer that houses the filtration module, and an air bubble supply unit that supplies air bubbles to a lower portion of the filtration module.
The filtration apparatus is equipped with the filtration module, which has excellent hollow fiber membrane surface cleaning efficiency and excellent filtration ability, and the hollow fiber membranes can be cleaned by air scrubbing using an air bubble supply unit; hence, the filtration ability can be enhanced and the utilization rate can be increased.
Here, the “existence region” refers to the smallest in area among imaginary convex polygons (polygons with all inner angles smaller than 180°) that contain all hollow fiber membranes when viewed in the alignment direction of the hollow fiber membranes. The term “rectangular” refers to a quadrilateral with unequal adjacent sides and does not include squares.
The “average effective length” of the hollow fiber membranes refers to an average of the lengths of portions of the hollow fiber membranes exposed between the holding members. The “packing area ratio” refers to the area fraction of the inner side of the outer circumferential surfaces of the hollow fiber membranes and is an occupying ratio including the area of the inner cavities of the hollow fiber membranes.
[Details of Embodiments of the Present Invention]
The individual embodiments of the present invention will now be described in detail with reference to the drawings.
[Filtration Module]
A filtration module 1 illustrated in
<Hollow Fiber Membranes>
The hollow fiber membranes 2 are prepared by forming porous films, which allow water to penetrate through but not particles contained in feed liquid, into tubes.
The hollow fiber membranes 2 may contain a thermoplastic resin as a main component. Examples of the thermoplastic resin include polyethylene, polypropylene, polyvinylidene fluoride, ethylene-vinyl alcohol copolymers, polyamide, polyimide, polyetherimide, polystyrene, polysulfone, polyvinyl alcohol, polyphenylene ether, polyphenylene sulfide, acetylcellulose, polyacrylonitrile, and polytetrafluoroethylene (PTFE). Among these, Pa E, which has excellent chemical resistance, heat resistance, weather resistance, and flame resistance and is porous, is preferable and monoaxially or biaxially stretched PTFE is more preferable. The material for forming the hollow fiber membranes may contain other polymers and additives such as a lubricant and the like.
As illustrated in
The lower limit of the ratio (La/Lb) of the average length La of the existence region A in the long side direction to the average length Lb in the short side direction is 10, preferably 15, and more preferably 20. The upper limit of the ratio of the average length La of the existence region A in the long side direction to the average length Lb in the short side direction 50, is preferably 45, and more preferably 40. When the ratio of the average length La in the long side direction to the average length Lb in the short side direction is below the lower limit, the length in the short side direction is excessively large and air bubbles may not be supplied to the central portion of the bundle of the hollow fiber membranes and the area of the existence region A may become so small that a sufficient filtration area can no longer be obtained. In contrast, when the ratio of the average length La of the existence region A in the long side direction to the average length Lb in the short side direction exceeds the upper limit, the filtration module is excessively elongated in the long side direction and handling may become difficult.
The lower limit of the ratio (Lt/Lb) of the average effective length Lt of the hollow fiber membranes 2 to the average length Lb of the existence region A in the short side direction is 40, preferably 50, and more preferably 60. In contrast, the upper limit of the ratio of the average effective length Lt of the hollow fiber membranes 2 to the average length Lb of the existence region A in the short side direction is 200, preferably 150, and more preferably 120. When the ratio of the average effective length Lt of the hollow fiber membranes 2 to the average length Lb of the existence region A in the short side direction is below the lower limit, bending of the hollow fiber membranes 2 is excessively reduced, titubation of the hollow fiber membranes 2 caused by abrasion with air bubbles is insufficient, and air bubbles may not be supplied to the hollow fiber membranes 2 located at the center of the existence region A. In contrast, when the ratio of the average effective length Lt of the hollow fiber membranes 2 to the average length Lb of the existence region A in the short side direction exceeds the upper limit, bending of the hollow fiber membranes 2 is excessively increased and the filtration efficiency and cleaning efficiency may be degraded due to entanglement of the hollow fiber membranes 2 or the like.
The lower limit of the packing area ratio of the hollow fiber membranes 2 in the existence region A is preferably 20% and more preferably 30%. The upper limit of the packing area ratio of the hollow fiber membranes 2 in the existence region A is preferably 60% and more preferably 55%. When the packing area ratio of the hollow fiber membranes 2 is below the lower limit, the number of hollow fiber membranes 2 per unit area is decreased and sufficient filtration efficiency may not be obtained. In contrast, when the packing area ratio of the hollow fiber membranes 2 exceeds the upper limit, the gaps between the hollow fiber membranes 2 become excessively small and air bubbles may not be supplied to the hollow fiber membranes 2 on the inner side of the existence region A.
The average pitch Pa of the hollow fiber membranes 2 in the long side direction is preferably larger than the average pitch Pb in the short side direction. The lower limit of the ratio (Pa/Pb) of the average pitch Pa of the hollow fiber membranes 2 in the long side direction to the average pitch Pb in the short side direction is preferably 1.2 and more preferably 1.5. The upper limit of the ratio of the average pitch Pa of the hollow fiber membranes 2 in the long side direction to the average pitch Pb in the short side direction is preferably 2.5 and more preferably 2. When the ratio of the average pitch Pa of the hollow fiber membranes 2 in the long side direction to the average pitch Pb in the short side direction is below the lower limit, sufficient air bubbles may not be introduced into the gaps between the hollow fiber membranes 2 in the short side direction of the existence region A. In contrast, when the ratio of the average pitch Pa of the hollow fiber membranes 2 in the long side direction to the average pitch Pb in the short side direction exceeds the upper limit, the density of the hollow fiber membranes 2 in the long side direction is decreased and filtration ability may become insufficient.
The lower limit of the number of hollow fiber membranes 2 arranged in the short side direction in the existence region A is preferably 8 and more preferably 12. The upper limit of the hollow fiber membranes 2 arranged in the short side direction is preferably 50 and more preferably 40. When the number of hollow fiber membranes 2 arranged in the short side direction is below the lower limit, the filtration area per facility area may not be sufficiently obtained. In contrast, when the number of hollow fiber membranes 2 arranged in the short side direction exceeds the upper limit, it becomes difficult to supply air bubbles to the central portion of the bundle of the hollow fiber membranes 2 in the short side direction and sufficient cleaning effect may not be obtained.
The lower limit of the ratio of the average pitch Pb in the short side direction to the average outer diameter of the hollow fiber membranes 2 is preferably 1. The upper limit of the ratio of the average pitch Pb in the short side direction to the average outer diameter of the hollow fiber membranes 2 is preferably 1.5 and more preferably 1.4. When the ratio of the average pitch Pb in the short side direction to the average outer diameter of the hollow fiber membranes 2 is below the lower limit, the hollow fiber membranes 2 are arranged to be in a squashed state in the radial direction, thereby posing a difficulty in manufacturing. In contrast, when the ratio of the average pitch Pb in the short side direction to the average outer diameter of the hollow fiber membranes 2 exceeds the upper limit, the density of the hollow fiber membranes 2 in the long side direction is decreased and thus filtration ability may become insufficient.
The lower limit of the average outer diameter of the hollow fiber membranes 2 is 1 mm, preferably 1.5 mm and more preferably 2 mm. The upper limit of the average outer diameter of the hollow fiber membranes 2 is 6 mm, preferably 5 mm, and more preferably 4 mm. When the average outer diameter of the hollow fiber membranes 2 is below the lower limit, the mechanical strength of the hollow fiber membranes 2 may become insufficient. In contrast, when the average outer diameter of the hollow fiber membranes 2 exceeds the upper limit, the flexibility of the hollow fiber membranes 2 becomes insufficient and thus vibrations and titubation of the hollow fiber membranes 2 caused by contact with air bubbles become insufficient. As a result, the gaps between the hollow fiber membranes 2 may not expand and air bubbles may not be introduced to the hollow fiber membranes 2 located on the inner side of the existence region A; moreover, the ratio of the surface area to the cross-sectional area of the hollow fiber membranes 2 may decrease and the filtration efficiency may decrease.
The lower limit of the average inner diameter of the hollow fiber membranes 2 is preferably 0.3 mm, more preferably 0.5 mm, and yet more preferably 0.9 mm. The upper limit of the average inner diameter of the hollow fiber membranes 2 is preferably 4 mm and more preferably 3 mm. When the average inner diameter of the hollow fiber membranes 2 is below the lower limit, pressure drop during the process of discharging the filtrated liquid inside the hollow fiber membranes 2 may increase. In contrast, when the average inner diameter of the hollow fiber membranes 2 exceeds the upper limit, the thickness of the hollow fiber membranes 2 is decreased and mechanical strength and impurity permeation preventing effect may become insufficient.
The lower limit of the ratio of the average inner diameter to the average outer diameter of the hollow fiber membranes 2 is preferably 0.3 and more preferably 0.4. The upper limit of the ratio of the average inner diameter to the average outer diameter of the hollow fiber membranes 2 is preferably 0.8 and more preferably 0.6. When the ratio of the average inner diameter to the average outer diameter of the hollow fiber membranes 2 is below the lower limit, the thickness of the hollow fiber membranes 2 increases excessively and the permeability of the hollow fiber membranes 2 may be degraded. In contrast, when the ratio of the average inner diameter to the average outer diameter of the hollow fiber membranes 2 exceeds the upper limit, the thickness of the hollow fiber membranes 2 decreases and the mechanical strength and impurity permeation preventing effect may become insufficient.
The lower limit of the average effective length of the hollow fiber membranes 2 is preferably 1 m and more preferably 2m. The upper limit of the average effective length of the hollow fiber membranes 2 is preferably 6 m and more preferably 5 m.
When the average effective length of the hollow fiber membranes 2 is below the lower limit, titubation of the hollow fiber membranes 2 caused by abrasion with air bubbles is insufficient and the gaps between the hollow fiber membranes 2 may not expand to allow air bubbles to reach the hollow fiber membranes 2 located on the inner side of the existence region. In contrast, when the average effective length of the hollow fiber membranes 2 exceeds the upper limit, the hollow fiber membranes 2 may undergo excessive bending due to their own weight and handling ease of installing the filtration module 1 etc., may be degraded.
The lower limit of the ratio (aspect ratio) of the average effective length to the average outer diameter of the hollow fiber membranes 2 is preferably 150 and more preferably 1000. The upper limit of the aspect ratio of the hollow fiber membranes 2 is preferably 6000 and more preferably 5000. When the aspect ratio of the hollow fiber membranes 2 is below the lower limit, the thickness of the bundle of the hollow fiber membranes 2 in the short side direction increases and the effect of introducing air bubbles in the short side direction into the inner side of the bundle of the hollow fiber membranes 2 caused by titubation of the hollow fiber membranes 2 may become insufficient. In contrast, when the aspect ratio of the hollow fiber membranes 2 exceeds the upper limit, the hollow fiber membranes 2 are excessively oblong and thus mechanical strength may decrease when the hollow fiber membranes 2 are held taut in vertical directions.
The lower limit of the porosity of the hollow fiber membranes 2 is preferably 70% and more preferably 75%. The upper limit of the porosity of the hollow fiber membranes 2 is preferably 90% and more preferably 85%. When the porosity of the hollow fiber membranes 2 is below the lower limit, permeability is degraded and the filtration ability of the filtration module 1 may be degraded. In contrast, when the porosity of the hollow fiber membranes 2 exceeds the upper limit, the mechanical strength and abrasion resistance of the hollow fiber membranes 2 may become insufficient. The porosity refers to the ratio of the total volume of pores to the volume of the hollow fiber membranes 2 and can be determined by measuring the density of the hollow fiber membranes 2 according to ASTM-D-792.
The lower limit of the area occupying ratio of the pores in the hollow fiber membranes 2 is preferably 40%. The upper limit of the area occupying ratio of the pores in the hollow fiber membranes 2 is preferably 60%. When the area occupying ratio of the pores is below the lower limit, permeability may be degraded and the filtration ability of the filtration module 1 may be degraded. In contrast, when the area occupying ratio of the pores exceeds the upper limit, the surface strength of the hollow fiber membranes 2 may be insufficient and rupture or the like of the hollow fiber membranes 2 may occur due to abrasion with air bubbles. The area occupying ratio refers to the ratio of the total area of the pores in the outer circumferential surfaces (filtration layer surfaces) of the hollow fiber membranes 2 relative to the surface area of the hollow fiber membranes 2 and can be determined by analyzing an electron micrographic image of the outer circumferential surfaces of the hollow fiber membranes 2.
The lower limit of the average diameter of the pores of the hollow fiber membranes 2 is preferably 0.01 μm. The upper limit of the average diameter of the pores of the hollow fiber membranes 2 is preferably 0.45 μm and more preferably 0.1 μm. When the average diameter of the pores of the hollow fiber membranes 2 is below the lower limit, permeability may be degraded. When the average diameter of the pores of the hollow fiber membranes 2 exceeds the upper limit, permeation of the impurities contained in the feed liquid into the interior of the hollow fiber membranes 2 may not be prevented. The average diameter of the pores refers to the average diameter of the pores in the outer circumferential surfaces (surfaces of filtration layers) of the hollow fiber membranes 2 and can be measured with a pore size distribution analyzer (for example, a porous material automatic pore size distribution measuring system available from Porous Materials Incorporated).
The lower limit of the tensile strength of the hollow fiber membranes 2 is preferably 50 N and more preferably 60 N. When the tensile strength of the hollow fiber membranes 2 is below the lower limit, durability to withstand surface cleaning with air bubbles may be degraded. The upper limit of the tensile strength of the hollow fiber membranes 2 is typically 150 N. The tensile strength refers to a maximum tensile stress observed in a tensile test conducted according to JIS K 7161 (1994) at a gauge length of 100 mm and a test speed of 100 mm/min.
The hollow fiber membranes 2 preferably have a multilayer structure. For example, as illustrated in
The materials constituting the support layer 2a and the filtration layer 2b may contain polytetrafluoroethylene (PTFE) as a main component. When the main component of the materials that constitute the support layer 2a and the filtration layer 2b is PTFE, the hollow fiber membranes 2 exhibit excellent mechanical strength and damage and the like on the surface of the hollow fiber membranes resulting from abrasion with air bubbles are reduced.
The lower limit of the number-average molecular weight of PTFE used in the support layer 2a and the filtration layer 2b is preferably 500,000 and more preferably 2,000,000. The upper limit of the number-average molecular weight of PTFE used in the support layer 2a and the filtration layer 2b is preferably 20,000,000. When the number-average molecular weight of PTFE is below the lower limit, the surfaces of the hollow fiber membranes 2 may be damaged by abrasion with air bubbles and mechanical strength of the hollow fiber membranes 2 may be degraded. When the number-average molecular weight of PTFE exceeds the upper limit, it may become difficult to form pores in the hollow fiber membranes 2.
The support layer 2a may be a tube prepared by extrusion-molding PTFE, for example. When an extrusion-molded tube is used as the support layer 2a, the support layer 2a exhibits mechanical strength and pores can be easily formed. This tube is preferably stretched at a stretch ratio of 50% or more and 700% or less in the axial direction and 5% or more and 100% or less in the circumferential direction.
The temperature for stretch is preferably not higher than the melting point of the tube material, for example, 0° C. or higher and 300° C. or lower. In order to obtain a porous material that includes pores having a relatively large diameter, low-temperature stretch is preferable. In order to obtain a porous material that includes pores having a relatively small diameter, high-temperature stretch is preferable. The stretched porous material is heat-treated at a temperature of 200° C. or higher and 300° C. or lower for, for example, 1 to 30 minutes while both ends are fixed to keep the stretched state; as a result, high dimensional stability is obtained. The size of the pores of the porous material can be adjusted by the combination of conditions such as stretch temperature, stretch ratio, etc.
The tube that forms the support layer 2a can be obtained by, for example, adding a liquid lubricant, such as naphtha, to PTFE fine powder, extrusion-molding the resulting mixture into a tube, and stretching the tube. Dimensional stability can be improved when the tube is held at a temperature not lower than the melting point of the PTFE fine powder, for example, 350° C. or higher and 550° C. or lower, in a heating furnace for several tens of seconds to several minutes to conduct sintering.
The average thickness of the support layer 2a is preferably 0.1 mm or more and 3 mm or less. When the average thickness of the support layer 2a is within this range, the hollow fiber membranes 2 strike good balance between mechanical strength and permeability.
The filtration layer 2b can be formed by, for example, wrapping a PTFE sheet around the support layer 2a and performing sintering. When a sheet is used as a material for forming the filtration layer 2b, stretch can be facilitated, the shape and size of pores can be easily adjusted, and the thickness of the filtration layer 2b can be decreased. Since the sheet is wrapped around and sintered, the support layer 2a and the filtration layer 2b become integral and the pores in these layers can be caused to connect to one another to improve permeability. The sintering temperature is preferably not lower than the melting point of the sheet that forms a tube for forming the support layer 2a and the sheet that forms the filtration layer 2b.
The sheet that forms the filtration layer 2b can be obtained by, for example, (1) a method with which an unsintered molded body obtained by extrusion of resin is stretched at a temperature not lower than the melting temperature and then sintered or (2) a method with which a sintered resin molded body is slowly cooled to increase crystallinity and the resulting cooled sintered molded body is stretched. This sheet is preferably stretched at a stretch ratio of 50% or more and 1000% or less in a longitudinal direction and 50% or more and 2500% or less in a transversal direction. In particular, when the stretch ratio in the transversal direction is within this range, the mechanical strength in the circumferential direction as the sheet is wrapped around can be improved and durability that withstands the surface cleaning with air bubbles can be improved.
When the filtration layer 2b is made by wrapping a sheet around the tube that forms the support layer 2a, fine irregularities are preferably formed on the outer circumferential surface of the tube. When irregularities are formed on the outer circumferential surface of the tube, misalignment with the sheet can be prevented, adhesion between the tube and the sheet can be improved, and detachment of the filtration layer 2b from the support layer 2a due to air bubble cleaning can be prevented. The number of times the sheet is wrapped around can be adjusted according to the thickness of the sheet. The number of times may be one or more than one. More than one sheets may be wrapped around the tube. The method for wrapping the sheet is not particularly limited. The sheet may be wrapped in the circumferential direction of the tube or may be spirally wrapped.
The height (level difference) in the fine irregularities is preferably 20 μm or more and 200 μm or less.
The fine irregularities are preferably formed in all parts of the outer circumferential surface of the tube but may be formed in some parts only or intermittently. Examples of the method for forming the fine irregularities on the tube outer circumferential surface include a surface treatment that uses flame, laser irradiation, plasma irradiation, and dispersion coating of a fluororesin or the like. The surface treatment that uses flame is preferable since irregularities can be easily formed without affecting the tube physical properties.
Alternatively, an unsintered tube and an unsintered sheet may be used and sintering may be conducted after the sheet is wrapped around the tube so as to increase adhesion between the tube and the sheet.
The average thickness of the filtration layer 2b is preferably 5 μm or more and 100 μm or less. When the average thickness of the filtration layer 2b is within this range, high filtration ability can be given to the hollow fiber membranes 2 easily and assuredly.
<Upper Holding Member>
The upper holding member 3 is a member that holds upper ends of the hollow fiber membranes 2 and has a discharge portion (water collecting header) that is in communication with inner cavities of the hollow fiber membranes 2 and collects the filtered liquid. A discharge duct is connected to this discharge portion so that the filtered liquid penetrated into the interior of the hollow fiber membranes 2 is discharged. The outer shape of the upper holding member 3 is not particularly limited. For example, the cross-sectional shape may be polygonal or circular.
As illustrated in
The bundle of the hollow fiber membranes 2 may be divided into two or more parts.
Examples of the material for the hollow casing 3a include resin compositions that contain PTFE, vinyl chloride, polyethylene, ABS resin, or the like as a main component.
The resin composition 3b may be any resin composition that has high adhesion to the hollow fiber membranes 2 and the hollow casing 3a and is capable of being cured within the hollow casing 3a. In particular, when hollow fiber membranes 2 composed of PTFE are used, the main component of the resin composition 3b is preferably an epoxy resin or a urethane resin capable of reliably preventing detachment of the hollow fiber membranes 2 and having high adhesion to the PTFE. When the hollow casing 3a is filled with the resin composition 3b, space between the hollow fiber membranes 2 and the side wall of the hollow casing 3a can be hermetically sealed. As a result, the discharge portion inside the upper holding member 3 and the outer side of the hollow fiber membranes 2 can be reliably separated and thus contamination of the filtered liquid with unfiltered feed liquid can be prevented.
The lower limit of the average filling thickness of the resin composition 3b in the direction of the alignment of the hollow fiber membranes 2 is preferably 20 mm and more preferably 30 mm. The upper limit of the average filling thickness of the resin composition 3b is preferably 60 mm and more preferably 50 mm. When the average filling thickness of the resin composition 3b is below the lower limit, the gap between the hollow fiber membranes 2 and the side wall of the hollow casing 3a may not be sufficiently sealed and the hollow fiber membranes 2 may fall off from the layer of the resin composition 3b. In contrast, when the average charging thickness of the resin composition 3b exceeds the upper limit, the size and weight of the upper holding member 3 may increase without necessity.
The lower holding member 4 is a holding member that holds lower ends of the hollow fiber membranes 2. The lower holding member 4 may have a similar structure to the upper holding member 3 or may be without a discharge portion that seals the lower ends of the hollow fiber membranes 2. The material for the lower holding member 4 may be the same as that for the upper holding member 3.
The lower holding member 4 may have a structure in which one hollow fiber membrane 2 is bent in a U shape. In such a case, the upper holding member 3 holds both ends of the hollow fiber membranes 2.
In order to facilitate handling (transportation, installation, replacement, etc.) of the filtration module 1, the upper holding member 3 and the lower holding member 4 may be joined together with a joining member. Examples of the joining member include metal supporting rods and resin casings (outer cylinders).
[Advantages]
The filtration module 1 includes a plurality of hollow fiber membranes 2 that are held by being aligned in one direction and a pair of holding members, namely, an upper holding member 3 and a lower holding member 4, those fix both ends of the hollow fiber membranes 2. In the upper holding member 3 and the lower holding member 4 of the filtration module 1, an existence region A where the hollow fiber membranes 2 exist has a rectangular shape in a direction perpendicular to the direction in which the hollow fiber membranes 2 are aligned. The ratio of the average length La of the existence region A in the long side direction to the average length Lb of the existence region A in the short side direction is 15 or more and 50 or less. The average outer diameter of the hollow fiber membranes 2 is 1 mm or more and 6 mm or less. The ratio of the average effective length Lt of the hollow fiber membranes 2 between the upper holding member 3 and the lower holding member 4 to the average length Lb of the existence region A in the long side direction is 40 or more and 200 or less. Thus, according to the filtration module 1, even when the packing area ratio of the hollow fiber membranes 2 in the existence region A is increased to increase the filtration area, the hollow fiber membranes 2 undergo titubation by air bubbles since the average length Lb in the short side direction is small and the average effective length Lt of the hollow fiber membranes 2 is large. Thus, the gaps are enlarged and air bubbles can be supplied to the interior of the bundle of the hollow fiber membranes 2 to achieve an extensive air scrubbing effect. Therefore, the filtration module 1 has excellent cleaning efficiency for the surfaces of the hollow fiber membranes 2 and excellent filtration ability.
[Filtration Apparatus]
A filtration apparatus equipped with the filtration module 1 illustrated in
A filtration apparatus illustrated in
In the filtration apparatus, the multiple filtration modules 1 are arranged side-by-side while being spaced from one another in the short side direction. In other words, the drawing of
<Filtration Vessel>
The filtration vessel 11 stores the feed liquid so as to have the filtration modules 1 immersed in the feed liquid.
A frame formed of metal or the like may be placed in the filtration vessel 11 to support the filtration modules 1 and the air bubble supply unit 12. Examples of the material of the filtration vessel 11 include resin, metal and concrete.
<Air Bubble Supply Unit>
The air bubble supply unit 12 supplies, from below the filtration modules 1, air bubbles B that clean the surfaces of the hollow fiber membranes 2. These air bubbles B clean the surfaces of the hollow fiber membranes 2 as they move up, abrading the surfaces of the hollow fiber membranes 2.
The air bubble supply unit 12 together with the filtration modules 1 are immersed in the feed liquid stored in the filtration vessel 11 and supplies air bubbles B by continuously or intermittently discharging gas supplied from a compressor or the like through a supply duct (not shown).
The air bubble supply unit 12 may be any known aeration equipment. Examples of the aeration equipment include aeration equipment that uses a porous plate or porous tube in which a large number of pores are formed in a resin or ceramic plate or tube, jet-type aeration equipment that jets out gas from a diffuser or sparger, intermittent bubble jetting aeration equipment that intermittently jets out air bubbles, and a bubbling jet nozzle that jets out water stream mixed with air bubbles.
An example of the intermittent bubble jetting aeration equipment is a combination of a device that stores the gas continuously supplied from a compressor or the like through a gas supply duct (not illustrated) and intermittently discharges the gas after reaching a particular volume to supply air bubbles and a component, such as a mesh, that breakdown the supplied air bubbles.
The gas that forms air bubbles supplied from the air bubble supply unit 12 may be any inert gas and is preferably air from the viewpoint of operation cost.
[Advantages]
The filtration apparatus includes the filtration modules 1, the filtration vessel 11 that houses the filtration modules 1, and the air bubble supply unit 12 that supplies air bubbles from below the filtration modules 1. Thus, the feed liquid in the filtration vessel 11 can be filtered by using the filtration modules 1. Since air bubbles are supplied to the filtration modules 1 from the air bubble supply unit 12, the hollow fiber membranes 2 in the filtration modules 1 are air-scrubbed and maintain the filtration ability. In particular, since the cleaning effect on the filtration modules 1 with air bubbles is high, the filtration ability is also high and the utilization rate can be increased.
[Other Embodiments]
The embodiments disclosed herein are merely exemplary in all respects and should not be considered as limiting. The scope of the present invention is not limited to the structures of the embodiments described above but by the claims and is intended to include all modifications within the meaning and the scope of the claims and their equivalents.
The filtration module is applicable not only to the filtration apparatus of the immersion suction type described above but also to various filtration apparatuses such as pressured cross-flow filtration apparatuses.
In the filtration module, the upper holding member may seal the hollow fiber membranes and the lower holding member may have a discharge portion.
In the filtration apparatus, the number of filtration modules may be any number including 1.
When the filtration apparatus is equipped with multiple filtration modules, one air bubble supply unit may be provided below for each of the filtration modules or one air bubble supply unit capable of supplying air bubbles to the multiple filtration modules may be provided.
The filtration module and the filtration apparatus are suitable for use as solid-liquid separation treatment apparatuses in various field.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2014-219751 | Oct 2014 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/079016 | 10/14/2015 | WO | 00 |
