WO2011016514A1 - Reverse osmosis membrane module and water purification system having same mounted therein - Google Patents
Reverse osmosis membrane module and water purification system having same mounted therein Download PDFInfo
- Publication number
- WO2011016514A1 WO2011016514A1 PCT/JP2010/063278 JP2010063278W WO2011016514A1 WO 2011016514 A1 WO2011016514 A1 WO 2011016514A1 JP 2010063278 W JP2010063278 W JP 2010063278W WO 2011016514 A1 WO2011016514 A1 WO 2011016514A1
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- WIPO (PCT)
- Prior art keywords
- reverse osmosis
- water
- osmosis membrane
- side spacer
- membrane module
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
- C02F1/003—Processes for the treatment of water whereby the filtration technique is of importance using household-type filters for producing potable water, e.g. pitchers, bottles, faucet mounted devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/10—Accessories; Auxiliary operations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
- B01D65/022—Membrane sterilisation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/14—Specific spacers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/14—Specific spacers
- B01D2313/143—Specific spacers on the feed side
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/168—Use of other chemical agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/34—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling by radiation
- B01D2321/343—By UV radiation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
Definitions
- the present invention relates to a reverse osmosis membrane module and a water purification system incorporating the same.
- the produced purified water is temporarily stored in a purified water tank, and is taken out from the purified water tank for use.
- the water purification system is provided with a chemical solution tank for cleaning and disinfecting the reverse osmosis membrane module and the purified water tank, and the microorganisms are disinfected by cleaning and disinfecting the reverse osmosis membrane module with a chemical solution. Is prevented from being blocked by microorganisms.
- an object of the present invention is to obtain a reverse osmosis membrane module that can easily prevent the reverse osmosis membrane from being blocked by microorganisms and to obtain a water purification system that can be always used.
- a reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water supply side spacer disposed outside the reverse osmosis membrane
- a reverse osmosis membrane module for separating the feed water introduced into the water supply side spacer into the permeate water and the concentrated water, wherein the water supply side spacer is blended with an antibacterial and antifungal agent.
- a reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water feed side spacer disposed outside the reverse osmosis membrane,
- a reverse osmosis membrane module for separating feed water introduced into a spacer into permeate and concentrated water, wherein the water supply side spacer is formed of a light transmitting member, and the UV light is irradiated to the water supply side spacer Is provided.
- FIG. 1 is a partially exploded perspective view of a reverse osmosis membrane module according to a first embodiment of the present invention.
- FIG. 2 is a perspective view showing an assembling procedure of the main part of the reverse osmosis membrane module shown in FIG. 1 in order from (a) to (c).
- FIG. 3 is a whole block diagram which shows an example of the water purification system in which a reverse osmosis membrane module is integrated.
- FIG. 4 is a partially exploded perspective view of a reverse osmosis membrane module according to a second embodiment of the present invention.
- the reverse osmosis membrane module 1 according to this embodiment is incorporated in a water purification system P that produces purified water from raw water, as shown in FIG. 3.
- the water purification system P used in the present embodiment is mainly used as a device for purifying potable water, and the first pre-filter 2A, the first activated carbon filter 2B and the second pre-filter 2A are used.
- a pretreatment device 2 comprising a filter 2C, a pump 3 disposed between the first prefilter 2A and the first activated carbon filter 2B, the reverse osmosis membrane module 1, the water purification tank 4, and a second And an activated carbon filter 5.
- the tap water (raw water) introduced to the water purification system P through the piping Pa is removed by the first prefilter 2A (about 5 um) and then pressurized by the pump 3 to remove the first waste water. It is sent to the activated carbon filter 2B. At this time, residual chlorine is removed, and fine particles are removed by the next second prefilter 2C (about 1 um) to perform pretreatment of the raw water.
- the feed water whose pretreatment has been completed is supplied from the primary side flow passage 6a of the on-off valve 6 to the water supply port 1a of the reverse osmosis membrane module 1, and the permeated water (clean water) filtered by the reverse osmosis membrane module 1 It is fed from the outlet 1 b to the pipe Pb via the secondary side flow passage 6 b of the on-off valve 6.
- the piping Pb is branched into a path leading to the water purification tank 4 and a path leading to the second activated carbon filter 5 and the faucet 7, and the purified water treated by the reverse osmosis membrane module 1 is supplied to the water purification tank 4
- the water is supplied from the faucet 7 through the second activated carbon filter 5.
- the concentrated water which has not been filtered by the reverse osmosis membrane module 1 is discharged from the concentrated water discharge port 1 c through the pipe Pc.
- the pressure switch 8 is provided in the pipe Pb
- the check valve 9 is provided in the secondary side flow passage 6b of the on-off valve 6, and the throttling valve 10 is provided in the pipe Pc.
- the pressure switch 8 detects and the pump 3 stops.
- the secondary flow passage 6b of the on-off valve 6 is maintained at high pressure by the check valve 9, but the water pressure of the primary flow passage 6a is discharged to the piping Pc for discharging concentrated water.
- the water pressure gradually decreases because When the pressure difference between the secondary flow passage 6b of the on-off valve 6 and the primary flow passage 6a reaches a predetermined value, the valve provided inside the on-off valve 6 is pushed by the pressure of the secondary flow passage 6b. And the primary side flow path 6a is shut off.
- the faucet 7 when the faucet 7 is opened, the water stored in the purified water tank 4 is supplied, whereby the water pressure in the secondary side flow passage 6b of the on-off valve 6 and the piping Pb drops, and the pressure is constant.
- the pressure switch 8 detects this and the pump 3 operates.
- the on-off valve 6 opens the one flow passage 6a, and the feed water passing through the pretreatment device 2 is supplied to the water supply port 1a of the reverse osmosis membrane module 1.
- the purified water discharged from the permeated water discharge port 1b is supplied from the faucet 7 through the secondary flow passage 6b and the pipe Pb.
- the reverse osmosis membrane module 1 is configured as shown in FIG. That is, the reverse osmosis membrane module 1 is configured to filter water by the reverse osmosis membrane 11, and as this reverse osmosis membrane 11, NF known as RO membrane (Reverse Osmosis Membrane) or nano filter generally known A membrane (Nanofiltration Membrane) etc. can be used.
- the reverse osmosis membrane 11 may be any membrane as long as it has a property of permeating water and impermeable to impurities other than water such as ions and salts, and is not limited to the RO membrane and the NF membrane.
- the reverse osmosis membrane module 1 is used in a state in which the reverse osmosis membrane 11 is wound.
- the reverse osmosis membrane 11 is formed in a bag shape in which only the center side to be wound is opened, and the reticulated permeate water side spacer 12 is inside the reverse osmosis membrane 11 in a bag shape.
- a mesh-like water supply side spacer 13 is arranged outside the reverse osmosis membrane 11 in the bag-like shape.
- the reverse osmosis membrane 11 is adhesively fixed to the water collection pipe 14 such that the open end of the reverse osmosis membrane 11 communicates with the inside of the water collection pipe 14 disposed at the center.
- the reverse osmosis membrane 11, the permeated water side spacer 12 and the water supply side spacer 13 are alternately stacked.
- the entire outermost periphery of the reverse osmosis membrane 11 in which the permeated water side spacer 12 and the water supply side spacer 13 are disposed is wound around the water collecting pipe 14, and the waterproof membrane 15 covers the entire outer periphery.
- FIGS. 2 (a) to 2 (c) show the process of winding the reverse osmosis membrane 11, the permeated water side spacer 12 and the water supply side spacer 13 around the water collecting pipe.
- a slit 14a for inserting the open side of the reverse osmosis membrane 11 formed in a bag shape is formed in the axial direction of the water collection tube 14 on the outer periphery of the water collection tube 14.
- the open side edge part of the reverse osmosis membrane 11 and the permeated water side spacer 12 which were pressed is inserted in the slit 14a, and it adhere
- the water supply side spacer 13 is attached to the outside of the bag-like reverse osmosis membrane 11, and these are wound around the water collection pipe 14. Thereafter, the outermost periphery is covered in a watertight manner with the waterproof film 15 (see FIG. 1) described above.
- the reverse osmosis membrane 11, the permeated water side spacer 12, and the water supply side spacer 13 are shown in FIG. 2, a plurality of sets may be provided and wound as shown in FIG.
- the first lid 16 is formed with a closed portion 16a at the central portion that closes the one end of the water collection pipe 14, and the supply ports 1a are radially formed around the closed portion 16a.
- the supply ports 1a are radially formed around the closed portion 16a.
- the second lid 17 is formed with a permeated water discharge port 1b communicating with the other end of the water collection pipe 14 at the central portion, and a concentrated water discharge port 1c is formed radially around the permeated water discharge port 1b. ing. As described above, by radially forming the concentrated water discharge port 1 c, the entire circumference of the other end side of the water supply side spacer 13 is communicated with the concentrated water discharge port 1 c.
- the function of the reverse osmosis membrane module 1 thus configured is as follows.
- the feed water pretreated by the pretreatment device 2 is introduced from the feed port 1a, the feed water is supplied to the entire periphery on one end side of the feed water side spacer 13 with a constant pressure, and then the water feed side spacer 13 And move in the direction of the concentrated water outlet 1c. While the feed water moves along the feed water side spacer 13, the water excluding the impurities in the feed water permeates the reverse osmosis membrane 11. Then, the permeated water (clean water) that has permeated the reverse osmosis membrane 11 is collected in the water collecting pipe 14 along the permeated water side spacer 12 in the bag-shaped reverse osmosis membrane 11 and moves inside the water collecting pipe 14 It is discharged from the permeated water discharge port 1b.
- the concentrated water containing the impurities which did not permeate the reverse osmosis membrane 11 is discharged from the concentrated water discharge port 1 c along the water supply side spacer 13.
- the permeated water side spacer 12 and the water supply side spacer 13 are provided in order to form a clearance gap between the wound reverse osmosis membranes 11, and to ensure a flow path.
- an antibacterial and antifungal agent is blended in the water supply side spacer 13 into which the supply water is introduced from the supply port 1a.
- the water supply side spacer 13 is made of a material such as polyester or polypropylene into which an antibacterial metal such as silver or copper or an antifungal agent (TBZ) is kneaded (a material containing an antibacterial / antifungal agent) Are formed in a net shape.
- the water permeable spacer 12 is formed in a net shape of a material such as polyester which does not contain an antibacterial and antifungal agent.
- the faucet 7 is closed and the water flow in the path of the water purification system P stagnates, and the water supply side spacer 13 is kneaded
- the incorporated antibacterial and antifungal agent is eluted in the water remaining in the arrangement of the water supply side spacer 13.
- the antibacterial / antifungal agent is compounded in the reticulated water supply side spacer 13 disposed outside the bag-like reverse osmosis membrane 11 ing. Therefore, when the water stagnates in the reverse osmosis membrane module 1, that is, when the faucet 7 is closed, the antibacterial and antifungal agent compounded in the water supply side spacer 13 remains in the water remaining in the arrangement of the water supply side spacer 13. Elute. And while it is suppressed that microorganisms proliferate by the water supply side spacer 13 by the eluted antibacterial and antifungal agent, the microbe which propagated by the water supply side spacer 13 can be bacterized. Therefore, it can be easily suppressed that the reverse osmosis membrane 11 is blocked by the microorganism.
- the antifungal agent does not permeate the reverse osmosis membrane 11, it is possible to prevent the antifungal agent from being mixed in the purified water. As a result, even immediately after water supply, since it can be used immediately without draining water, waste of water can be prevented.
- the permeated water side spacer 12 is disposed inside the reverse osmosis membrane 11, and the water supply side spacer 13 is disposed outside the reverse osmosis membrane 11, and the reverse osmosis membrane 11 is formed into a bag shape. While being fixed so as to communicate the inside of the water collection pipe 14 with the open side end of the water collection pipe 14, it is wound around the water collection pipe 14, and the outermost periphery is covered watertight with a waterproof membrane 15.
- the reverse osmosis membrane module is attached by attaching the first lid 16 having the supply port 1a formed thereon and the second lid 17 having the permeated water outlet 1b and the concentrated water outlet 1c formed at the other end. Form one. Therefore, the reverse osmosis membrane module 1 can be made cylindrical, and can be easily incorporated into the water purification system P.
- the reverse osmosis membrane module 1 according to the present embodiment is incorporated into the water purification system P, there is no need to wash the reverse osmosis membrane module 1 using a chemical solution or the like, and a water purification system P that can be always used can be obtained. it can.
- the antibacterial agent is not conventionally used for the spacer by the side of water supply, the main reason is that the aromatic polyamide of a synthetic membrane is generally used as a material of a reverse osmosis membrane.
- This aromatic polyamide is weak to a high concentration of chlorine compounds and oxidizing agents, which may cause material deterioration.
- a reverse osmosis membrane is generally used for industrial use in many cases, it can also be mentioned as a factor that it is cheaper to periodically wash it than the cost of blending an antibacterial agent into a spacer.
- the antibacterial and antifungal agent it is preferable to use a silver-based antibacterial agent and an antifungal agent (TBZ) which are non-oxidative and act at a relatively low concentration, and by containing them in the water supply side spacer 13, It is possible to suppress the performance decrease due to the blockage of the reverse osmosis membrane 11 due to bacterial reproduction while making maintenance of the drug cleaning unnecessary.
- the water purification system can be used not only as a household water purification system P but also as an industrial water purification system.
- the reverse osmosis membrane module 1A is basically formed into a bag shape and wound, similarly to the reverse osmosis membrane module 1 of the first embodiment. 11; a mesh-like permeated water side spacer 12 disposed inside the bag-shaped reverse osmosis membrane 11; a mesh-like water supply spacer 13 disposed outside the bag-shaped reverse osmosis membrane 11; have.
- the present embodiment is mainly different from the first embodiment in that the water supply side spacer 13 is formed of a translucent member, and the water supply side spacer 13 is provided with a UV lamp 20 for irradiating ultraviolet light. It is in. Furthermore, in the present embodiment, an optical fiber is used as the light transmitting member.
- the UV lamp 20 is disposed such that ultraviolet light is irradiated to the water supply side spacer 13 formed of an optical fiber.
- one or more UV lamps 20 are provided so as to be in contact with the wound water-supply-side spacers 13, and the UV lamps 20 are wound together with the water-supply-side spacers 13 to supply water formed by optical fibers with ultraviolet light. It arranges so that side spacer 13 may be irradiated.
- the terminals 20a and 20b of the UV lamp 20 are projected from the water supply port 1a of the first lid 16, and the terminals 20a and 20b and the respective UV lamps 20 are electrically connected. There is.
- the UV lamps 20 are arranged to be in contact with the wound water-supply-side spacers 13, and the water-supply-side spacers 13 are formed of an optical fiber which is a translucent member. Can be widely distributed through the optical fiber of the wound water supply side spacer 13.
- the mesh-like water supply side spacer 13 disposed outside the bag-like reverse osmosis membrane 11 is formed of a light transmitting member, and UV is irradiated to the water supply side spacer 13 A lamp 20 is provided.
- the ultraviolet light emitted from the UV lamp 20 spreads over the wide area of the water supply side spacer 13 through the optical fiber (light transmitting member) of the water supply side spacer 13.
- the microbes propagated by the water supply side spacer 13 can be bacterized by ultraviolet light, and the reproduction of microbes in the water supply side spacer 13 formed outside the bag-like reverse osmosis membrane 11 can be suppressed. Therefore, it can be easily suppressed that the reverse osmosis membrane 11 is blocked by the microorganism.
- permeability of the ultraviolet-ray irradiated from the UV lamp 20 can be raised by using an optical fiber as a translucent member. Therefore, ultraviolet rays can be spread over a wider range of the water supply side spacer 13, and the bacteriostatic efficiency of the water supply side spacer 13 can be further enhanced.
- a reverse osmosis membrane module capable of preventing the reverse osmosis membrane from being blocked by microorganisms, and to obtain a water purification system that can be always used.
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- Life Sciences & Earth Sciences (AREA)
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Abstract
Description
本発明は、逆浸透膜モジュールおよびこれを組み込んだ浄水システムに関する。 The present invention relates to a reverse osmosis membrane module and a water purification system incorporating the same.
従来、浄水システムとして、原水タンクから送られる原水中の残留塩素を活性炭フィルタで除去した後、軟水化手段によって軟水化し、軟水化した原水を逆浸透膜モジュールで濾過して精製水を作り出したものが知られている(たとえば、特許文献1参照)。 Conventionally, as a water purification system, residual chlorine in raw water sent from a raw water tank is removed with an activated carbon filter, then softened by a water softening means, and the softened raw water is filtered by a reverse osmosis membrane module to create purified water Are known (see, for example, Patent Document 1).
この特許文献1の浄水システムでは、作り出された精製水を精製水タンクに一旦貯留して、精製水タンクから取り出して使用するようになっている。
In the water purification system of
さらに、特許文献1では、浄水システムに、逆浸透膜モジュールおよび精製水タンクを洗浄・消毒する薬液タンクを設け、薬液により逆浸透膜モジュールを洗浄・消毒することで微生物を殺菌し、逆浸透膜が微生物によって閉塞されてしまうのを抑制している。
Furthermore, in
しかしながら、かかる従来の浄水システムにあっては、薬液を使用した後に配管内を洗浄する必要があり、洗浄作業に多くの手間が掛かってしまう。また、薬液の使用時および使用後の洗浄時には浄水システムを休止する必要があるため、常時使用することができないという問題があった。 However, in such a conventional water purification system, it is necessary to clean the inside of the pipe after using the chemical solution, and it takes a lot of labor for the cleaning operation. Moreover, since it is necessary to stop a water purification system at the time of the washing | cleaning at the time of use and after use of a chemical | medical solution, there existed a problem that it could not always use.
そこで、本発明は、逆浸透膜が微生物によって閉塞されるのを容易に抑制することのできる逆浸透膜モジュールを得るとともに常時使用することのできる浄水システムを得ることを目的とする。 Then, an object of the present invention is to obtain a reverse osmosis membrane module that can easily prevent the reverse osmosis membrane from being blocked by microorganisms and to obtain a water purification system that can be always used.
本発明にあっては、袋状に形成された逆浸透膜と、当該逆浸透膜の内側に配置される透過水側スペーサと、前記逆浸透膜の外側に配置される給水側スペーサと、を有し、給水側スペーサに導入された供給水を透過水と濃縮水とに分離する逆浸透膜モジュールであって、前記給水側スペーサに、抗菌・抗カビ剤を配合したことを特徴とする。 In the present invention, a reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water supply side spacer disposed outside the reverse osmosis membrane And a reverse osmosis membrane module for separating the feed water introduced into the water supply side spacer into the permeate water and the concentrated water, wherein the water supply side spacer is blended with an antibacterial and antifungal agent.
また、袋状に形成された逆浸透膜と、当該逆浸透膜の内側に配置される透過水側スペーサと、前記逆浸透膜の外側に配置される給水側スペーサと、を有し、給水側スペーサに導入された供給水を透過水と濃縮水とに分離する逆浸透膜モジュールであって、前記給水側スペーサを透光性部材で形成するとともに、当該給水側スペーサに紫外線を照射するUVランプを設けたことを特徴とする。 Moreover, it has a reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water feed side spacer disposed outside the reverse osmosis membrane, A reverse osmosis membrane module for separating feed water introduced into a spacer into permeate and concentrated water, wherein the water supply side spacer is formed of a light transmitting member, and the UV light is irradiated to the water supply side spacer Is provided.
本発明によれば、逆浸透膜が微生物により閉塞されてしまうのを容易に抑制することができる。 ADVANTAGE OF THE INVENTION According to this invention, it can suppress easily that a reverse osmosis membrane is obstruct | occluded by microorganisms.
以下、本発明の実施形態について図面を参照しながら詳細に説明する。なお、以下の複数の実施形態には、同様の構成要素が含まれている。よって、以下では、それら同様の構成要素には共通の符号を付与するとともに、重複する説明を省略する。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. In addition, the same component is contained in several following embodiments. Therefore, in the following, those similar components are given the same reference numerals, and redundant explanations are omitted.
(第1実施形態)
本実施形態にかかる逆浸透膜モジュール1は、図3に示すように、原水から浄水を作り出す浄水システムPに組み込まれている。
First Embodiment
The reverse
具体的には、本実施形態で用いる浄水システムPは、主として家庭用の飲料水を浄化する装置として用いられるものであり、第1のプレフィルタ2A、第1の活性炭フィルタ2Bおよび第2のプレフィルタ2Cからなる前処理装置2と、第1のプレフィルタ2Aと第1の活性炭フィルタ2Bとの間に配置されるポンプ3と、前記逆浸透膜モジュール1と、浄水タンク4と、第2の活性炭フィルタ5と、を備えている。
Specifically, the water purification system P used in the present embodiment is mainly used as a device for purifying potable water, and the first pre-filter 2A, the first activated
そして、配管Paを介して浄水システムPに導入される水道水(原水)は、第1のプレフィルタ2A(約5um)で粗ゴミが除去された後、ポンプ3で加圧されて第1の活性炭フィルタ2Bに送られる。ここで残留塩素が除去されるとともに、次の第2のプレフィルタ2C(約1um)で微粒子が除去されて原水の前処理が行われる。
Then, the tap water (raw water) introduced to the water purification system P through the piping Pa is removed by the
前処理が完了した供給水は、開閉弁6の一次側流路6aから逆浸透膜モジュール1の給水口1aに供給され、逆浸透膜モジュール1で濾過された透過水(浄水)は透過水吐出口1bから開閉弁6の二次側流路6bを介して配管Pbに送給される。配管Pbは、浄水タンク4に通ずる経路と、第2の活性炭フィルタ5および蛇口7に通ずる経路と、に分岐しており、逆浸透膜モジュール1で処理された浄水は、浄水タンク4に給水されるとともに第2の活性炭フィルタ5を通過して蛇口7から給水されるようになっている。一方、逆浸透膜モジュール1で濾過されなかった濃縮水は、濃縮水吐出口1cから配管Pcを介して排出される。
The feed water whose pretreatment has been completed is supplied from the primary side flow passage 6a of the on-off
また、配管Pbには圧力スイッチ8が設けられると共に、開閉弁6の二次側流路6bに逆止弁9が設けられており、配管Pcには絞り弁10が設けられている。
Further, the
そして、かかる構成とすることで浄水システムPは以下のように動作する。 And the water purification system P operate | moves as follows by setting it as this structure.
まず、蛇口7を閉めると、配管Pb内の浄水が浄水タンク4に給水されると同時に経路内の水圧が上昇し、一定の水圧に達すると圧力スイッチ8が検知してポンプ3が停止する。このようにポンプ3が停止すると、開閉弁6の二次側流路6bは逆止弁9により高圧が保持されるが、一次側流路6aの水圧は濃縮水を排出する配管Pcへと排出されるため水圧が徐々に低下する。そして、開閉弁6の二次側流路6bと一次側流路6aとの圧力差が所定値に達すると、開閉弁6の内部に設けられた弁が二次側流路6bの圧力で押されて一次側流路6aを遮断する。
First, when the faucet 7 is closed, the clean water in the piping Pb is supplied to the clean water tank 4 and the water pressure in the path rises at the same time, and when the constant water pressure is reached, the
次に、蛇口7を開けると、浄水タンク4内に溜められた水が供給されることにより、開閉弁6の二次側流路6bおよび配管Pb内の水圧が下降し、その圧力が一定の水圧よりも下がると圧力スイッチ8がこれを検知してポンプ3が作動する。また、二次側流路6bの圧力が低下することにより、開閉弁6が一側流路6aを開き、前処理装置2を経由した供給水が逆浸透膜モジュール1の給水口1aに供給され、透過水吐出口1bから吐出される浄水が二次側流路6bおよび配管Pbを介して蛇口7から給水される。このように、蛇口7を開・閉することでポンプ3が作動・停止するように浄水システムPを構成することで、浄水システムPが常に浄水供給可能な態勢となるようにしている。
Next, when the faucet 7 is opened, the water stored in the purified water tank 4 is supplied, whereby the water pressure in the secondary
ここで、逆浸透膜モジュール1は、図1に示すように構成されている。すなわち、逆浸透膜モジュール1は、逆浸透膜11によって水を濾過するようになっており、この逆浸透膜11としては、一般に知られるRO膜(Reverse Osmosis Menbrane)やナノフィルターと称されるNF膜(Nanofiltration Membrane)などを用いることができる。なお、逆浸透膜11は、水を透過しイオンや塩類などの水以外の不純物を透過しない性質を有する膜であればよく、RO膜、NF膜に限られるものではない。
Here, the reverse
本実施形態では、逆浸透膜モジュール1は、逆浸透膜11を巻回した状態で用いられるようになっている。具体的には、逆浸透膜11は、巻回される中心側のみが開放される袋状に形成されており、袋状となった逆浸透膜11の内側に網状の透過水側スペーサ12が配置されるとともに、袋状となった逆浸透膜11の外側に網状の給水側スペーサ13が配置されている。そして、逆浸透膜11は、当該逆浸透膜11の開放側端部が中心に配置した集水管14の内部と連通するように、当該集水管14に接着固定されている。このとき、図1に示すように、逆浸透膜11、透過水側スペーサ12および給水側スペーサ13は、それらが交互に積層されるようになっている。
In the present embodiment, the reverse
そして、透過水側スペーサ12および給水側スペーサ13を配置した逆浸透膜11を集水管14に巻き付けた全体の最外周を防水性の膜15によって水密に被覆している。
Then, the entire outermost periphery of the
ここで、図2に基づいて、逆浸透膜モジュール1の製造方法の概略を説明する。図2(a)~(c)は、逆浸透膜11、透過水側スペーサ12および給水側スペーサ13を集水管14の周りに巻き付ける工程を示している。
Here, based on FIG. 2, the outline of the manufacturing method of the reverse
まず、図2(a)に示すように、帯状に形成した2枚の逆浸透膜11の間に透過水側スペーサ12を挟んだ状態で、2枚の逆浸透膜11の集水管14側を除いた3辺の周縁部どうしを接着剤Aで袋状に貼り合わせる。そして、図2(b)に示すように、2枚の逆浸透膜11および透過水側スペーサ12をプレスする。
First, as shown in FIG. 2A, with the permeate
一方、図2(a)に示すように、集水管14の外周には、袋状に形成した逆浸透膜11の開放側を挿入するスリット14aを集水管14の軸方向に形成しておく。そして、図2(b)に示すように、プレスした逆浸透膜11および透過水側スペーサ12の開放側端部をスリット14aに嵌め込んで接着する。
On the other hand, as shown in FIG. 2A, a
そして、図2(c)に示すように、袋状となった逆浸透膜11の外側に給水側スペーサ13を添えて、これらを集水管14の周りに巻き付ける。その後、上述した防水性の膜15(図1参照)で最外周を水密に被覆する。なお、図2では、1組の逆浸透膜11、透過水側スペーサ12および給水側スペーサ13を示したが、図1に示すように、それらを複数組設けて巻き付けるようにしてもよい。
Then, as shown in FIG. 2C, the water
このように、逆浸透膜11、透過水側スペーサ12および給水側スペーサ13を巻回して防水性の膜15で被覆することで、逆浸透膜モジュール1は、図1に示すように、全体として集水管14を中心とする円柱状に形成される。
Thus, by winding the
そして、集水管14の一端(図1中手前側)には、供給口1aを形成した第1の蓋体16が取り付けられるとともに、他端(図1中奥側)には、透過水吐出口1bおよび濃縮水吐出口1cを形成した第2の蓋体17が取り付けられる。
And while the
第1の蓋体16は、中心部に集水管14の一端を閉塞する閉塞部16aが形成されるとともに、供給口1aが閉塞部16aを中心として放射状に形成されている。このように、供給口1aを放射状に形成することで、給水側スペーサ13の一端側の全周が供給口1aに連通されるようにしている。
The
第2の蓋体17は、中心部に集水管14の他端に連通する透過水吐出口1bが形成されるとともに、その透過水吐出口1bを中心として濃縮水吐出口1cが放射状に形成されている。このように、濃縮水吐出口1cを放射状に形成することで、給水側スペーサ13の他端側の全周が濃縮水吐出口1cに連通されるようにしている。
The
かかる構成とした逆浸透膜モジュール1の機能は、以下のとおりである。
The function of the reverse
まず、前処理装置2で前処理された供給水が供給口1aから導入されると、当該供給水は一定の圧力をもって給水側スペーサ13の一端側全周に供給された後、給水側スペーサ13を伝って濃縮水吐出口1c方向へと移動する。この給水側スペーサ13を伝って供給水が移動する間に、供給水中の不純物を除く水が逆浸透膜11を透過する。すると、逆浸透膜11を透過した透過水(浄水)は袋状となった逆浸透膜11内の透過水側スペーサ12を伝って集水管14内に集められ、集水管14の内側を移動して透過水吐出口1bから吐出される。一方、逆浸透膜11を透過しなかった不純物を含む濃縮水は、給水側スペーサ13を伝って濃縮水吐出口1cから排出される。なお、透過水側スペーサ12および給水側スペーサ13は、巻回された逆浸透膜11間に隙間を形成して流路を確保するために設けるものである。
First, when the feed water pretreated by the
ここで、本実施形態では、供給口1aから供給水が導入される給水側スペーサ13に、抗菌・抗カビ剤を配合している。具体的には、給水側スペーサ13は、銀や銅などの抗菌性金属、または、抗カビ剤(TBZ)を練り込んだポリエステル、ポリプロピレンなどの材料(抗菌・抗カビ剤が配合された材料)を用いて、網状に形成されている。一方、透水側スペーサ12は、抗菌・抗カビ剤を含有しないポリエステルなどの材料で網状に形成されている。
Here, in the present embodiment, an antibacterial and antifungal agent is blended in the water
このように、給水側スペーサ13に、抗菌・抗カビ剤を配合することで、蛇口7を閉めて浄水システムPの経路内の水の流れが停滞した状態のときに、給水側スペーサ13に練り込んだ抗菌・抗カビ剤が、給水側スペーサ13の配置内に残存した水に溶出することになる。
Thus, by mixing the antibacterial and antifungal agent into the water
以上、説明したように、本実施形態の逆浸透膜モジュール1によれば、袋状となった逆浸透膜11の外側に配置される網状の給水側スペーサ13に抗菌・抗カビ剤を配合している。そのため、逆浸透膜モジュール1内で水が停滞した状態、つまり、蛇口7を閉じた状態では、給水側スペーサ13に配合した抗菌・抗カビ剤が給水側スペーサ13の配置内に残存した水に溶出される。そして、溶出した抗菌・抗カビ剤によって給水側スペーサ13で微生物が繁殖するのが抑制されるとともに、給水側スペーサ13で繁殖した微生物を静菌できるようになる。そのため、逆浸透膜11が微生物により閉塞されてしまうのを容易に抑制することができるようになる。
As described above, according to the reverse
また、抗菌・抗カビ剤は逆浸透膜11を透過しないため、抗菌・抗カビ剤が浄水に混入されるのを避けることができる。その結果、給水直後であっても捨て水をすること無く直ちに使用できるため、水が無駄になるのを防止することができる。
In addition, since the antifungal agent does not permeate the
また、本実施形態によれば、逆浸透膜11の内側に透過水側スペーサ12を配置するとともに当該逆浸透膜11の外側に給水側スペーサ13を配置し、袋状となった逆浸透膜11の開放側端部を集水管14の内部と連通するように固定した状態で当該集水管14の周りに巻き付けるとともに、最外周を防水性の膜15によって水密に被覆し、集水管14の一端側に、供給口1aを形成した第1の蓋体16を取り付けるとともに、他端に、透過水吐出口1bおよび濃縮水吐出口1cを形成した第2の蓋体17を取り付けることで逆浸透膜モジュール1を形成している。そのため、逆浸透膜モジュール1を円柱状にすることができ、浄水システムPに容易に組み込むことができるようになる。
Further, according to the present embodiment, the permeated
また、本実施形態にかかる逆浸透膜モジュール1を浄水システムPに組み込めば、薬液等を用いて逆浸透膜モジュール1を洗浄する必要がなくなり、常時使用することのできる浄水システムPを得ることができる。
Moreover, if the reverse
ところで、従来では給水側のスペーサに抗菌剤が使用されていないが、その主な理由としては、逆浸透膜の材料として一般には合成膜の芳香族ポリアミドが用いられていることがあげられる。この芳香族ポリアミドは高濃度の塩素化合物や酸化剤に弱く材料劣化する虞があるためである。また、逆浸透膜は一般的に産業用で使用されることが多いため、スペーサに抗菌剤を配合するコストよりも定期的に洗浄する方が安いということも一因としてあげることができる。 By the way, although the antibacterial agent is not conventionally used for the spacer by the side of water supply, the main reason is that the aromatic polyamide of a synthetic membrane is generally used as a material of a reverse osmosis membrane. This aromatic polyamide is weak to a high concentration of chlorine compounds and oxidizing agents, which may cause material deterioration. Moreover, since a reverse osmosis membrane is generally used for industrial use in many cases, it can also be mentioned as a factor that it is cheaper to periodically wash it than the cost of blending an antibacterial agent into a spacer.
なお、抗菌・抗カビ剤としては、非酸化系で比較的低濃度で作用する銀系抗菌剤および抗カビ剤(TBZ)を用いることが好ましく、それらを給水側スペーサ13に含有させることにより、薬剤洗浄のメンテナンスを不要としつつ細菌繁殖による逆浸透膜11の閉塞による性能低下を抑制することができる。また、浄水システムは、家庭用の浄水システムPとしてだけでなく、工業用の浄水システムとしても用いることができる。
As the antibacterial and antifungal agent, it is preferable to use a silver-based antibacterial agent and an antifungal agent (TBZ) which are non-oxidative and act at a relatively low concentration, and by containing them in the water
(第2実施形態)
本実施形態にかかる逆浸透膜モジュール1Aは、図4に示すように、基本的に上記第1実施形態の逆浸透膜モジュール1と同様に、袋状に形成されて巻回される逆浸透膜11と、袋状となった逆浸透膜11の内側に配置される網状の透過水側スペーサ12と、袋状となった逆浸透膜11の外側に配置される網状の給水側スペーサ13と、を有している。そして、給水側スペーサ13から供給される供給水が逆浸透膜11を透過することで生成される透過水は、透過水側スペーサ12を伝って透過水吐出口1bへと導かれる一方、逆浸透膜11を透過しない供給水は、濃縮水となって濃縮水吐出口1cへと導かれる。
Second Embodiment
As shown in FIG. 4, the reverse
ここで、本実施形態が上記第1実施形態と主に異なる点は、給水側スペーサ13を透光性部材で形成するとともに、その給水側スペーサ13に紫外線を照射するUVランプ20を設けたことにある。さらに、本実施形態では、透光性部材として光ファイバーを用いている。
Here, the present embodiment is mainly different from the first embodiment in that the water
本実施形態では、UVランプ20は、紫外線が光ファイバーで形成された給水側スペーサ13に照射されるように配置されている。たとえば、巻回されたそれぞれの給水側スペーサ13に接するようにUVランプ20を1つまたは複数設け、当該UVランプ20を給水側スペーサ13と一緒に巻き込むことで、紫外線が光ファイバーで形成された給水側スペーサ13に照射されるように配置する。このとき、UVランプ20の端子20a、20bが第1の蓋体16の給水口1aから突出されるようになっており、それら端子20a、20bと各UVランプ20とが電気的に接続されている。
In the present embodiment, the
このように、UVランプ20を、巻回されたそれぞれの給水側スペーサ13に接するように配置するとともに、給水側スペーサ13を透光性部材である光ファイバーで形成することで、UVランプ20の紫外線を、巻回された給水側スペーサ13の光ファイバーを通って広範囲に行き渡らせることができるようになる。
As described above, the
以上の本実施形態によっても、上記第1実施形態と同様の作用、効果を奏することができる。 According to the above-described embodiment, the same operation and effect as those of the first embodiment can be achieved.
また、本実施形態によれば、袋状となった逆浸透膜11の外側に配置される網状の給水側スペーサ13を透光性部材で形成するとともに、給水側スペーサ13に紫外線を照射するUVランプ20を設けている。そのため、UVランプ20から照射された紫外線が給水側スペーサ13の光ファイバー(透光性部材)を通って給水側スペーサ13の広範囲に行き渡ることになる。その結果、給水側スペーサ13で繁殖した微生物を紫外線によって静菌でき、袋状となった逆浸透膜11の外側に形成される給水側スペーサ13における微生物の繁殖を抑制することができる。そのため、逆浸透膜11が微生物により閉塞されてしまうのを容易に抑制することができるようになる。
Further, according to the present embodiment, the mesh-like water
また、本実施形態によれば、透光性部材として光ファイバーを用いることで、UVランプ20から照射された紫外線の透過率を高めることができる。そのため、紫外線を給水側スペーサ13のより広範囲に行き渡らせることができ、給水側スペーサ13の静菌効率をより一層高めることができる。
Moreover, according to this embodiment, the transmittance | permeability of the ultraviolet-ray irradiated from the
以上、本発明の好適な実施形態について説明したが、本発明は上記実施形態には限定されず、種々の変形が可能である。たとえば、上記第1および第2実施形態にかかる逆浸透膜モジュールを、その他の浄水システムに組み込むことも可能である。 As mentioned above, although preferred embodiment of this invention was described, this invention is not limited to the said embodiment, A various deformation | transformation is possible. For example, it is also possible to incorporate the reverse osmosis membrane module according to the first and second embodiments into another water purification system.
本発明によれば、逆浸透膜が微生物によって閉塞されるのを抑制することのできる逆浸透膜モジュールを得るとともに常時使用することのできる浄水システムを得ることができる。 According to the present invention, it is possible to obtain a reverse osmosis membrane module capable of preventing the reverse osmosis membrane from being blocked by microorganisms, and to obtain a water purification system that can be always used.
Claims (6)
前記給水側スペーサに、抗菌・抗カビ剤を配合したことを特徴とする逆浸透膜モジュール。 A reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water supply side spacer disposed outside the reverse osmosis membrane A reverse osmosis membrane module for separating introduced feed water into permeate and concentrated water, comprising:
A reverse osmosis membrane module characterized in that an antibacterial and antifungal agent is blended in the water supply side spacer.
前記給水側スペーサを透光性部材で形成するとともに、当該給水側スペーサに紫外線を照射するUVランプを設けたことを特徴とする逆浸透膜モジュール。 A reverse osmosis membrane formed in a bag shape, a permeated water side spacer disposed inside the reverse osmosis membrane, and a water supply side spacer disposed outside the reverse osmosis membrane A reverse osmosis membrane module for separating introduced feed water into permeate and concentrated water, comprising:
A reverse osmosis membrane module characterized in that the water supply side spacer is formed of a translucent member and a UV lamp for irradiating the water supply side spacer with ultraviolet light is provided.
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| CN2010800350433A CN102470326A (en) | 2009-08-07 | 2010-08-05 | Reverse osmosis membrane module and water purification system having same mounted therein |
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| JP2009184073A JP2011036752A (en) | 2009-08-07 | 2009-08-07 | Reverse osmosis membrane module and water purification system incorporating the same therein |
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| Publication Number | Publication Date |
|---|---|
| WO2011016514A1 true WO2011016514A1 (en) | 2011-02-10 |
Family
ID=43544409
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2010/063278 Ceased WO2011016514A1 (en) | 2009-08-07 | 2010-08-05 | Reverse osmosis membrane module and water purification system having same mounted therein |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JP2011036752A (en) |
| KR (1) | KR20120049247A (en) |
| CN (1) | CN102470326A (en) |
| TW (1) | TW201129417A (en) |
| WO (1) | WO2011016514A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020079091A1 (en) * | 2018-10-16 | 2020-04-23 | Technische Universität Dresden | Membrane separating method and membrane module for processing liquids |
| WO2022161612A1 (en) * | 2021-01-28 | 2022-08-04 | Omify Ag | Tap-mounted water purification unit |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015009174A (en) * | 2013-06-27 | 2015-01-19 | 株式会社日立製作所 | Water treatment system and water treatment method for water treatment system |
| CN104355429B (en) * | 2014-11-10 | 2017-06-27 | 珠海格力电器股份有限公司 | Water purification system with antibacterial function |
| DE102017108535A1 (en) * | 2017-04-21 | 2018-10-25 | Grünbeck Wasseraufbereitung GmbH | Membrane module and device and method for the detection of deposits in a membrane module |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01123690A (en) * | 1987-11-06 | 1989-05-16 | Kazuhiko Kawamura | Method and device for cleaning water |
| JPH0724446A (en) * | 1993-07-14 | 1995-01-27 | Teac Corp | Water purifier |
| JP2001252543A (en) * | 2000-03-10 | 2001-09-18 | Toray Ind Inc | Reverse osmosis composite membrane |
| JP2001259384A (en) * | 2000-03-17 | 2001-09-25 | Kurita Water Ind Ltd | Spiral type membrane module cleaning method |
| JP2004243194A (en) * | 2003-02-13 | 2004-09-02 | Nomura Micro Sci Co Ltd | Membrane treatment apparatus for water treatment |
-
2009
- 2009-08-07 JP JP2009184073A patent/JP2011036752A/en not_active Ceased
-
2010
- 2010-08-05 KR KR1020127003111A patent/KR20120049247A/en not_active Ceased
- 2010-08-05 CN CN2010800350433A patent/CN102470326A/en active Pending
- 2010-08-05 WO PCT/JP2010/063278 patent/WO2011016514A1/en not_active Ceased
- 2010-08-06 TW TW099126294A patent/TW201129417A/en unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01123690A (en) * | 1987-11-06 | 1989-05-16 | Kazuhiko Kawamura | Method and device for cleaning water |
| JPH0724446A (en) * | 1993-07-14 | 1995-01-27 | Teac Corp | Water purifier |
| JP2001252543A (en) * | 2000-03-10 | 2001-09-18 | Toray Ind Inc | Reverse osmosis composite membrane |
| JP2001259384A (en) * | 2000-03-17 | 2001-09-25 | Kurita Water Ind Ltd | Spiral type membrane module cleaning method |
| JP2004243194A (en) * | 2003-02-13 | 2004-09-02 | Nomura Micro Sci Co Ltd | Membrane treatment apparatus for water treatment |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020079091A1 (en) * | 2018-10-16 | 2020-04-23 | Technische Universität Dresden | Membrane separating method and membrane module for processing liquids |
| WO2022161612A1 (en) * | 2021-01-28 | 2022-08-04 | Omify Ag | Tap-mounted water purification unit |
| WO2022162070A1 (en) * | 2021-01-28 | 2022-08-04 | Omify | Tap-mounted water purification unit |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102470326A (en) | 2012-05-23 |
| KR20120049247A (en) | 2012-05-16 |
| JP2011036752A (en) | 2011-02-24 |
| TW201129417A (en) | 2011-09-01 |
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