WO2011151883A1 - Power recovery device of liquid treatment apparatus - Google Patents
Power recovery device of liquid treatment apparatus Download PDFInfo
- Publication number
- WO2011151883A1 WO2011151883A1 PCT/JP2010/059220 JP2010059220W WO2011151883A1 WO 2011151883 A1 WO2011151883 A1 WO 2011151883A1 JP 2010059220 W JP2010059220 W JP 2010059220W WO 2011151883 A1 WO2011151883 A1 WO 2011151883A1
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- WO
- WIPO (PCT)
- Prior art keywords
- pair
- peripheral surface
- central axis
- raw water
- chambers
- Prior art date
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 75
- 239000007788 liquid Substances 0.000 title claims abstract description 20
- 230000002093 peripheral effect Effects 0.000 claims abstract description 94
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 76
- 239000012528 membrane Substances 0.000 claims abstract description 51
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 50
- 238000003825 pressing Methods 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000012267 brine Substances 0.000 description 38
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 38
- 239000013535 sea water Substances 0.000 description 24
- 239000000203 mixture Substances 0.000 description 12
- 238000010612 desalination reaction Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 239000013505 freshwater Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000382 dechlorinating effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 239000002455 scale inhibitor Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D5/00—Blades; Blade-carrying members; Heating, heat-insulating, cooling or antivibration means on the blades or the members
- F01D5/02—Blade-carrying members, e.g. rotors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
- F03B—MACHINES OR ENGINES FOR LIQUIDS
- F03B13/00—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
- F05B2220/00—Application
- F05B2220/60—Application making use of surplus or waste energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
- F05B2220/00—Application
- F05B2220/60—Application making use of surplus or waste energy
- F05B2220/602—Application making use of surplus or waste energy with energy recovery turbines
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/50—Hydropower in dwellings
Definitions
- Embodiments of the present invention relate to a power recovery apparatus for a liquid processing apparatus.
- a liquid processing apparatus that processes water containing a plurality of components (hereinafter referred to as raw water) using a reverse osmosis membrane called an RO membrane is known.
- Raw water is supplied to the reverse osmosis membrane at high pressure, and water is extracted from the raw water in the reverse osmosis membrane. Meanwhile, the ratio of water extracted by the reverse osmosis membrane tends to increase as the pressure value of the raw water supplied to the reverse osmosis membrane increases.
- the strength of the raw water pressure raising device necessary to increase the pressure value of the raw water must be increased, and the amount of energy required for improving the pressure of the raw water also increases.
- the configuration of the raw water pressure raising device is also complicated.
- the raw water after the water is extracted at a certain rate in the reverse osmosis membrane (herein, the high concentration raw water) loses some of its pressure due to the extraction of the water in the reverse osmosis membrane.
- the raw water maintains most of the high pressure that was loaded on the raw water when it was supplied to the reverse osmosis membrane.
- the high-pressure energy maintained by the high-concentration raw water is recovered with high efficiency and the pressure of new raw water supplied to the reverse osmosis membrane is increased with a simple configuration, and the high-pressure raw water is supplied to the reverse osmosis membrane at high pressure.
- a power recovery device for a liquid processing apparatus that can reduce the amount of new external energy required for increasing the pressure of new raw water, and thus can reduce the amount of energy required for operation of the liquid processing apparatus, that is, the power. Is to provide.
- a power recovery device for a liquid processing apparatus sends raw water, which is water supplied from the outside and contains a plurality of components, to a reverse osmosis membrane via a pressure increase unit, and then water from the raw water in the reverse osmosis membrane. Used in a liquid processing apparatus for extracting a part of the raw water, and the raw water whose pressure has been increased by using the pressure of the remaining raw water after the water is partially extracted in the reverse osmosis membrane is added to the raw water from the pressure increasing unit. Power recovery device that feeds the reverse osmosis membrane.
- the power recovery apparatus includes: a housing having an internal space; a central shaft having an outer peripheral surface fixed to the internal space of the housing and projecting to the outside of the housing; and a center in the internal space of the housing An inner peripheral surface that is rotatably accommodated around the outer peripheral surface of the shaft and that faces the outer peripheral surface of the central shaft, and an outer peripheral surface that is located radially outward of the central shaft, and so on in the circumferential direction of the central shaft A rotating member including a plurality of passages arranged at intervals and each extending between an inner peripheral surface and an outer peripheral surface.
- At least one set of two-to-one set chambers facing the outer peripheral surface of the rotating member and partitioned from each other is provided.
- the central axis is formed on the outer peripheral surface of the central axis and faces at least one pair of chambers in the internal space of the housing via a rotating member, and has at least one pair of two-to-one sets equal to the number of the chambers, and at least one A two-to-one pair of passages extending from the pair of openings in the central axis and opening at the at least one end of the central axis are formed.
- One pair of chambers arranged symmetrically with respect to the central axis in the pair of chambers in the internal space of the housing is introduced with the raw water introduced from the outside by introducing the raw water supplied from the outside.
- the rotating member is configured to rotate by pressing against a plurality of passages on the outer peripheral surface of the rotating member exposed in the pair of chambers in a predetermined circumferential direction of the outer peripheral surface.
- the other pair of chambers arranged symmetrically with respect to the central axis in the pair of chambers are connected to the raw water passage between the pressure raising unit and the reverse osmosis membrane.
- One pair of openings opposed to the one pair of chambers through the rotating member in the pair of openings on the outer peripheral surface of the central axis is connected to the outside through one pair of passages corresponding to the central axis. It is communicated to.
- the other pair of openings facing the other pair of chambers through the rotating member in the pair of openings on the outer peripheral surface of the central axis is connected to the other pair of passages corresponding to the central axis via the other pair of passages.
- the remaining raw water is introduced.
- FIG. 1 is a diagram schematically showing an entire example of a liquid processing apparatus in which a power recovery apparatus according to the first embodiment of the present invention is used.
- FIG. 2 is a perspective view schematically showing the external appearance of the power recovery apparatus according to the first embodiment of the present invention.
- FIG. 3 is a schematic exploded perspective view of the power recovery device of FIG. 2.
- FIG. 4 is a schematic perspective view from below of the case with the central axis of the power recovery device of FIG.
- FIG. 5 is a perspective view schematically showing a horizontal cross section of the rotating member of the power recovery apparatus of FIG. 3.
- FIG. 6 is a schematic perspective view of the central axis of the power recovery apparatus of FIG.
- FIG. 7 is a schematic perspective view of a lower portion after the central axis of FIG.
- FIG. 6 is cut along line IV-IV.
- 8 is an exploded perspective view similar to FIG. 3 for explaining the operation of the power recovery apparatus of FIG.
- FIG. 9 is a schematic plan view of a combination of the case of FIG. 8, the central shaft, and the rotating member for explaining the operation of the power recovery apparatus of FIG.
- FIG. 10 is a schematic exploded perspective view of a power recovery apparatus according to the second embodiment of the present invention.
- FIG. 11 is a perspective view showing a half of the rotating member of the power recovery device of FIG. 10 in a horizontal section.
- FIG. 12 is a perspective view of the central axis of FIG.
- FIG. 13 is a schematic perspective view of the lower part after the central axis of FIG. 12 is cut along the line XIII-XIII.
- FIG. 14 is a schematic perspective view of the lower end portion after further cutting the lower portion of the central axis in FIG. 13 along the line XIV-XIV.
- An example of a liquid processing apparatus is a seawater desalination apparatus.
- the raw water that is supplied from the outside and contains a plurality of components is seawater.
- Seawater SW pumped up from the sea is supplied to the pretreatment unit 10.
- the pretreatment unit 10 performs pretreatment by adding, for example, a bactericide 10a, a flocculant 10b, a scale inhibitor 10c, a dechlorinating agent 10d, and the like to the seawater SW supplied thereto.
- the pretreated seawater (pretreated seawater) PSW is guided by a pipe so as to pass through the water pump 12 and the security filter 14.
- the pretreated seawater PSW after passing through the security filter 14 is branched into two by a branch pipe.
- One branch pipe is connected to the reverse osmosis membrane unit 18 storing the reverse osmosis membrane 18a through the pressure raising unit 16.
- the pressure raising unit 16 is provided by a high pressure pump.
- the pretreated seawater PSW loaded with a predetermined high pressure by the pressure raising unit 16 is sent to the reverse osmosis membrane unit 18 through one branch pipe.
- a part of the water (fresh water) FW is extracted from the high-pressure pretreated seawater HPSW by the reverse osmosis membrane unit 18 in the reverse osmosis membrane unit 18.
- Extracted water FW is guided to the water purification tank 20 by piping.
- a hardness adjusting agent 20 a, a ph adjusting agent 20 b, a disinfecting agent 20 c, and the like are added to the water FW to create the purified water CW.
- the purified water CW created in the purified water tank 20 is supplied to the water pipe 23 via the purified water supply pump 22.
- the other branch pipe is connected to the power recovery device 24 according to the first embodiment.
- the low-pressure pretreatment seawater PSW sent to the power recovery device 24 via the other branch pipe is called a low-pressure feed LPF.
- Seawater (high-concentration seawater) in which a part of the water FW is extracted in the reverse osmosis membrane unit 18 and the concentration of various components including salt is increased and the pressure is somewhat reduced is led to the power recovery device 24 by piping. ing.
- High-concentration seawater sent from the reverse osmosis membrane unit 18 to the power recovery device 24 is called high-pressure brine HPB.
- the power recovery device 24 increases the pressure of the low-pressure feed LPF by increasing the pressure of the high-pressure brine HPB with the energy of the low-pressure feed LPF and then the high-pressure brine HPB having the increased pressure pushes out the low-pressure feed LPF. And discharged as a high-pressure feed HPF. That is, the energy of the high pressure feed HPF is generated by using a part of the energy of the low pressure feed LPF in addition to using most of the energy of the high pressure brine HPB. ing.
- the high-pressure feed HPF is led from the power recovery device 24 to a pipe between the pressure raising unit 16 and the reverse osmosis membrane unit 18 by a pipe.
- the high-pressure feed HPF is added to the high-pressure pretreated seawater HPSW from the pressure increasing unit 16 toward the reverse osmosis membrane unit 18 in this pipe, and goes to the reverse osmosis membrane unit 18 together with the high-pressure pretreated seawater HPSW.
- the low-pressure feed LPF after being used to increase the pressure of the high-pressure brine HPB in the power recovery device 24 further increased the pressure using a part of the energy of the low-pressure feed LPF in the next cycle.
- the pressure is increased by the high-pressure brine HPB to become a high-pressure feed HPF.
- the high-pressure brine HPB increases the pressure of the low-pressure feed LPF, then loses the pressure, and is discharged from the power recovery device 24 to the outside as the low-pressure brine LPB.
- the power recovery device 24 includes a housing 32 having an internal space 30 as shown in FIGS.
- the housing 32 includes a case 32a having a substantially circular recess that provides the internal space 30, and a lid 32b that liquid-tightly covers an opening on one side of the recess of the case 32a.
- the lid 32b is detachably fixed to the case 32a by known fixing means (not shown).
- the power recovery device 24 further includes a central shaft 34 that is fixed to the internal space 30 of the housing 32 and has an outer peripheral surface and at least one end protruding outside the housing 32.
- the central shaft 34 is elongated, and a part of the outer peripheral surface thereof is liquid-tightly fixed to a through hole 32c formed at the center of the bottom surface of the recess of the case 32a.
- One end portion of the central shaft 34 located on one side along the longitudinal center line of the central shaft 34 projects from the through hole 32c into the external space below the case 32a.
- the other end portion of the central axis 34 located on the other side along the longitudinal center line projects from the through hole 32d at the center of the lid 32b into the external space above the lid 32b.
- the power recovery device 24 also includes a rotating member 36 that is housed in the inner space 30 of the housing 32 so as to be rotatable around the outer peripheral surface of the central shaft 34.
- the rotating member 36 has an inner peripheral surface 36a facing the outer peripheral surface of the central shaft 34 and an outer peripheral surface 36b positioned radially outward of the central shaft 34, as shown in FIG. It includes a plurality of passages 36c that are arranged at equal intervals in the circumferential direction of the shaft 34 and each extend between the inner peripheral surface 36a and the outer peripheral surface 36b.
- the internal space 30 of the housing 32 is provided with at least one pair of chambers 38 a and 38 b that are two-to-one and face each other and face the outer peripheral surface 36 b of the rotating member 36. It has been.
- a pair of chambers 38a and 38b are provided.
- a pair of chambers 38a disposed symmetrically with respect to the central axis 34 are provided with power as shown in FIG.
- the low pressure feed LPF supplied to the recovery device 24 is introduced as shown in FIG.
- One pair of chambers 38a has a predetermined circumferential direction of the outer peripheral surface 36b with respect to the outer peripheral surface 36b of the rotating member 36 exposing the introduced low-pressure feed LPF in the one pair of chambers 38a (in FIG. 3). It is shaped to follow (counterclockwise direction).
- the other pair of chambers 38b arranged symmetrically with respect to the central axis 34 is supplied with pressure from the power recovery device 24 as shown in FIGS. It is connected to a pipe for high pressure feed HPF that goes to the pipe between the ascending unit 16 and the reverse osmosis membrane unit 18.
- the central shaft 34 is formed on the outer peripheral surface of the central shaft 34, and at least one pair of chambers 38 a and 38 b in the inner space 30 of the housing 32 is interposed via a rotating member 36. At least one pair of openings 40a and 40b, which are the same number as the chambers 38a and 38b. In this embodiment, two-to-one sets of openings 40 a and 40 b are formed on the outer peripheral surface of the central shaft 34 at equal intervals in the circumferential direction of the outer peripheral surface.
- a pair of passages 42a extend to the portion, and the pair of passages 42a open to the end face of the other end.
- the pair of passages 42a can be integrated into the central shaft 34 before reaching the other end as shown in FIGS.
- the opening of the integrated passage 42a at the end face of the other end of the central shaft 34 is connected to a conduit for the low pressure brine LPB extending from the power recovery device 24 as shown in FIGS. Has been.
- a pair of passages 42b extends to the end, and the pair of passages 42b opens at the end face of the one end.
- the pair of passages 42b can be integrated into the central shaft 34 before reaching the one end as shown in FIG.
- the opening of the integrated passage 42b at the end face of one end of the central shaft 34 is made of high-pressure brine HPB extending from the reverse osmosis membrane unit 18 toward the power recovery device 24 as shown in FIGS. Is connected to the pipeline.
- the high-pressure brine HPB fed from the reverse osmosis membrane unit 18 shown in FIG. 1 toward the power recovery device 24 is connected to the central shaft 34 of the power recovery device 24 as shown in FIGS.
- the other pair of openings 40b on the outer peripheral surface of the central shaft 34 is reached via a passage 42b (see FIG. 4) that opens to the end face of the lower end portion, and the other one of the plurality of passages 36c of the rotating member 36 It flows into some of the passages 36c with the inner ends exposed at the pair of openings 40b.
- the low pressure feed LPF sent from the pretreatment unit 10 shown in FIG. 1 to the power recovery device 24 via the water pump 12 and the safety filter 14 is shown in FIGS.
- the air flows into the pair of chambers 38 a of the case 32 a of the housing 32 of the power recovery device 24.
- the low-pressure feed LPF that has flowed into the pair of chambers 38a has a predetermined circumference on the outer circumferential surface of the rotating member 36 with respect to the portion of the outer circumferential surface of the rotating member 36 exposed in the pair of chambers 38a. Pressed along the direction.
- the low-pressure feed LPF in one pair of chambers 38a has the side surfaces of several passages 36c that expose the outer ends in one pair of chambers 38a in the plurality of passages 36c of the rotating member 36. It flows into these several passages 36c while pushing. A part of the energy of the low-pressure feed LPF is consumed to rotate the rotating member 36 in the predetermined direction R.
- the low pressure feed LPF in the passage 36c is located between one pair of chambers 38a and the other pair of chambers 38b, and one pair of openings 40a and the other opening 40b of the central shaft 34.
- the high-pressure brine HPB flowing into the passage 36c from the other opening 40b are pushed into a pair of chambers 38b.
- the pressure energy of the high-pressure brine HPB that has flowed into the passage 36c from the opening 40b is applied to the low-pressure feed LPF in the passage 36c, and the low-pressure feed LPF in the passage 36c becomes the high-pressure feed HPF. Extruded.
- the high-pressure brine HPB that has flowed into the passage 36c from the other opening 40b gives pressure energy to the low-pressure feed LPF in the passage 36c, and the pressure energy is greatly reduced or eliminated to become the low-pressure brine LPB.
- the central shaft is driven by the low-pressure feed LPF that is confined to the pair of chambers 38a and the pair of openings 40a of the central shaft 34 and then flows into the passage 36c from the pair of chambers 38a.
- 34 is discharged to the outside of the power recovery device 24 through one pair of passages 42a corresponding to one pair of openings 40a.
- the high-pressure feed HPF in the other pair of chambers 38b is led from the power recovery device 24 to the piping between the pressure increasing unit 16 and the reverse osmosis membrane unit 18 by piping as shown in FIG.
- the high-pressure feed HPF is added to the high-pressure pretreated seawater HPSW from the pressure increasing unit 16 toward the reverse osmosis membrane unit 18 in this pipe, and goes to the reverse osmosis membrane unit 18 together with the high-pressure pretreated seawater HPSW.
- the amount of fresh water FW extracted in the reverse osmosis membrane unit 18 per unit time is constant, the high pressure that must be sent from the pressure increase unit 16 toward the reverse osmosis membrane unit 18 per unit time.
- the amount of pretreated seawater HPSW can be reduced. This can reduce the amount of energy required for the operation of the seawater desalination apparatus, which is a kind of liquid processing apparatus using the power recovery device 24, that is, the power.
- the two-to-one set of chambers 38a and 38b provided in the internal space 30 of the case 32a of the housing 32 are mutually separated with the central shaft 34 interposed therebetween.
- the same low-pressure feed LPF is introduced into one pair of chambers 38a arranged symmetrically with respect to each other, and at the same time, the same with the other pair of chambers 38b arranged symmetrically with respect to each other across the central axis 34.
- High pressure brine HPB has been introduced.
- the low pressure feed LPF in one pair of chambers 38a and the rotating member 36 rotatably accommodated in the case 32a of the housing 32 and the inner space 30 of the case 32a with respect to the outer peripheral surface of the central shaft 34
- the force applied by the high pressure brine HPB in the other pair of chambers 38 b is canceled in the radial direction of the central shaft 34.
- the mixture of the low-pressure brine LPB and the high-pressure brine HPB that have entered the gap between the outer peripheral surface of the central shaft 34 and the inner peripheral surface 36 a of the rotating member 36 causes the rotation of the rotating member 36 on the outer peripheral surface of the central shaft 34. Accordingly, it functions as a radial dynamic pressure bearing between the outer peripheral surface of the central shaft 34 and the inner peripheral surface 36 a of the rotating member 36. Further, the area excluding the two-to-one pair of chambers 38a and 38b on the inner peripheral surface facing the outer peripheral surface 36b of the rotating member 36 in the inner space 30 of the case 32a of the housing 32 and the outer peripheral surface 36b of the rotating member 36.
- an independent radial bearing is not required between the outer peripheral surface of the central shaft 34 and the inner peripheral surface 36a of the rotating member 36, and the configuration of the power recovery device 24 of this embodiment can be simplified and the manufacturing cost can be reduced. I can do it.
- the low-pressure brine LPB that has entered a gap between the inner surface of the lid 32b of the housing 32 and one side surface of the rotating member 36 in the inner space 30 of the case 32a of the housing 32 that faces the inner surface.
- the mixture of the high-pressure brine HPB and the mixture of the low-pressure feed LPF and the high-pressure feed HPF is formed between the inner surface of the lid 32b and the one side surface of the rotary member 36 as the rotary member 36 rotates on the outer peripheral surface of the central shaft 34. It functions as a thrust bearing.
- the low pressure brine that has entered the gap between the lower surface of the internal space 30 of the case 32a of the housing 32 and the other side surface of the rotating member 36 in the internal space 30 of the case 32a of the housing 32 facing the bottom surface A mixture of LPB and high-pressure brine HPB and a mixture of low-pressure feed LPF and high-pressure feed HPF are produced by the rotation of the rotary member 36 on the outer peripheral surface of the central shaft 34 and the other surface of the internal space 30 of the case 32a and the other side of the rotary member 36. Acts as a thrust bearing between the sides.
- an independent thrust bearing is not required between the inner surface of the lid 32b and the one side surface of the rotating member 36 and between the lower surface of the internal space 30 of the case 32a and the other side surface of the rotating member 36.
- the configuration of the power recovery device 24 of this embodiment can be simplified and the manufacturing cost can be reduced.
- the power recovery device 24 ′ includes a housing 43 having an internal space 41 as shown in FIGS. 10 to 14.
- the housing 43 includes a case 43a having a substantially circular recess that provides the internal space 41, and a lid 43b that liquid-tightly covers the opening on one side of the recess of the case 43a.
- the lid 43b is detachably fixed to the case 43a by known fixing means (not shown).
- the power recovery device 24 ′ includes a central shaft 44 that protrudes from the center of the inner space 41 of the housing 43 to the outer space above the lid 43 b through the central through-hole 43 c of the lid 43 b.
- the central shaft 44 is elongated, and a part of the outer peripheral surface thereof is liquid-tightly fixed to the central through hole 43c of the lid 43b.
- One end of the central shaft 44 located on one side along the longitudinal center line of the central shaft 44 protrudes from the through hole 43c of the lid 43b to the external space above the lid 32b.
- the other end of the central shaft 44 located on the other side along the longitudinal center line is located slightly above the center of the bottom surface of the internal space 41 of the housing 43.
- the power recovery device 24 ′ also includes a rotating member 46 that is rotatably accommodated in the inner space 41 of the housing 43 around the outer peripheral surface of the other end portion of the central shaft 44.
- a bottomed hole 46 a that receives the other end of the central shaft 44 is formed in the center of the rotating member 46.
- the inner peripheral surface 46b and the bottom surface of the bottomed hole 46a face the outer peripheral surface and the end surface of the other end of the central shaft 44 received in the bottomed hole 46a so as to be rotatable relative to each other.
- the rotating members 46 are arranged at equal intervals in the circumferential direction of the bottom hole 46a as shown in FIG. 11 and the outer peripheral surface 46c positioned radially outward of the bottom hole 46a.
- a plurality of passages 46d extending between the surface 46b and the outer peripheral surface 46c are included.
- the internal space 41 of the housing 43 is provided with at least one pair of chambers 48a and 48b that are two-to-one and face each other and face the outer peripheral surface 46c of the rotating member 46. It has been.
- a two-to-one set of chambers 48a, 48b is provided.
- one pair of chambers 48a disposed symmetrically with respect to the central axis 44 is connected to the power recovery device 24 'in FIG.
- the low pressure feed LPF being supplied is introduced as shown in FIG.
- One pair of chambers 48a has a predetermined circumferential direction of the outer peripheral surface 46c (in FIG. 10) with respect to the outer peripheral surface 46c of the rotating member 46 exposing the introduced low-pressure feed LPF in the one pair of chambers 48a. It is shaped to follow (counterclockwise direction).
- the other pair of chambers 48b arranged symmetrically with respect to the central axis 44 is connected to the power recovery device 24 'as shown in FIGS. It is connected to a pipe for high pressure feed HPF that goes to the pipe between the pressure raising unit 16 and the reverse osmosis membrane unit 18.
- the center shaft 44 has at least one set of chambers in the inner space 41 of the housing 43 formed on the outer peripheral surface of the other end portion of the center shaft 44 as well shown in FIGS. 10 and 12 to 14.
- 48a and 48b are opposed to each other with the rotation member 46 therebetween, and at least one pair of openings 50a and 50b of the same number as the chambers 48a and 48b is formed.
- two-to-one sets of openings 50a and 50b are formed on the outer peripheral surface of the other end portion of the central shaft 44 at equal intervals in the circumferential direction of the outer peripheral surface.
- the center axis 44 is located above the central axis 44 toward the one end.
- a pair of passages 52a extends, and the pair of passages 52a are open at the end face of the one end.
- the pair of passages 52a can be integrated into the central shaft 44 until reaching the one end as shown in FIGS.
- the opening of the integrated passage 52a at the end face of the one end of the central shaft 44 is a low-pressure brine extending from the power recovery device 24 (24 'in this embodiment) as shown in FIGS. It is connected to the pipeline for LPB.
- the inside of the central shaft 44 is directed to the one end located above the central shaft 44.
- a pair of passages 52b extends, and the pair of passages 52b open to the end face of the one end.
- the pair of passages 52b can be integrated into one in the central shaft 44 before reaching the one end as shown in FIGS.
- the pair of passages 52b are concentrically integrated with the integrated passage 52a as described above on the end face of the one end portion of the central shaft 44.
- the opening of the integrated passage 52b at the end face of the one end portion of the central shaft 44 extends from the reverse osmosis membrane unit 18 to the power recovery device 24 (24 ′ in this embodiment) as shown in FIGS. Is connected to the line for the high-pressure brine HPB extending to
- a through hole 43d is formed in the center of the bottom surface of the internal space 41 of the housing 43 of this embodiment (ie, the bottom surface of the case 42a), and the output shaft 54a of the motor 54 is rotatable and liquid-tight in the through hole 43d. Has been inserted.
- Such a rotatable and liquid-tight insertion of the output shaft 54a of the motor 54 is, for example, an O-ring or an oil seal between the inner peripheral surface of the through hole 43d and the outer peripheral surface of the output shaft 54a of the motor 54. This is possible by interposing a known annular sealing member.
- the protruding end of the output shaft 54 a of the motor 54 inserted into the through hole 43 d is concentrically fixed from the outside to the bottom wall of the bottom hole 46 a in the center of the rotating member 46 in the internal space 41 of the housing 43.
- the high pressure brine HPB sent out from the reverse osmosis membrane unit 18 shown in FIG. 1 toward the power recovery device 24 (24 ′ in this embodiment) is a power recovery device 24 as shown in FIG.
- the other pair of openings 50b flows into some of the passages 46d in which the inner ends are exposed.
- the low-pressure feed LPF that has flowed into the pair of chambers 48a has a predetermined circumference on the outer peripheral surface of the rotating member 46 with respect to the portion of the outer peripheral surface of the rotating member 46 exposed in the pair of chambers 48a. Pressed along the direction.
- the low-pressure feed LPF in one pair of chambers 48a has the side surfaces of several passages 46d exposing the outer ends in one pair of chambers 48a in the plurality of passages 46d of the rotating member 46. It flows into these several passages 46d while pushing. A part of the energy of the low pressure feed LPF is consumed to rotate the rotating member 46 in the predetermined direction R.
- the low pressure feed LPF in the passage 46d is between one pair of chambers 48a and the other pair of chambers 48b, and one pair of openings 50a and the other opening 50b of the central shaft 44. Between the passage 46d and the other pair of chambers 48b and the other opening 50b of the central shaft 44 by the high-pressure brine HPB flowing into the passage 46d from the other opening 50b. Into a pair of chambers 48b.
- the high-pressure brine HPB that has flowed into the passage 46d from the other opening 50b gives pressure energy to the low-pressure feed LPF in the passage 46d so that the pressure energy is greatly reduced or eliminated to become the low-pressure brine LPB.
- 36 further rotation in the passage 46d between the other pair of chambers 48b and one pair of chambers 48a and between the other pair of openings 50b and one pair of openings 50a in the central shaft 44. And then the central shaft by the low-pressure feed LPF that flows from one pair of chambers 58a into the passage 56d when corresponding to one pair of chambers 48a and one pair of openings 50a of the central shaft 44.
- One pair of openings 50a of 44 is discharged to the outside of the power recovery device 24 (24 ′ in this embodiment) through one pair of corresponding passages 52a.
- the high pressure feed HPF in the other pair of chambers 48b is connected to the pressure raising unit 16 and the reverse osmosis membrane unit by piping from the power recovery device 24 (24 'in this embodiment) as shown in FIGS. 18 to the pipe between the two.
- the high-pressure feed HPF is added to the high-pressure pretreated seawater HPSW from the pressure increasing unit 16 toward the reverse osmosis membrane unit 18 in this pipe, and goes to the reverse osmosis membrane unit 18 together with the high-pressure pretreated seawater HPSW.
- the amount of fresh water FW extracted in the reverse osmosis membrane unit 18 per unit time is constant, the high pressure that must be sent from the pressure increase unit 16 toward the reverse osmosis membrane unit 18 per unit time.
- the amount of pretreated seawater HPSW can be reduced. This can reduce the amount of energy required for the operation of the seawater desalination apparatus, which is a kind of liquid processing apparatus using the power recovery apparatus 24 (24 ′ in this embodiment), that is, power.
- the rotation of the rotating member 46 in the inner space 41 of the housing 43 can be controlled using the motor 54.
- the power recovery device 24 ′ provides the high pressure feed HPF that is led from the power recovery device 24 ′ to the piping between the pressure increasing unit 16 and the reverse osmosis membrane unit 18 by the rotation of the rotating member 46.
- the amount of energy applied can be controlled independently of the value of the rotational force applied to the rotating member 46 by the low pressure feed LPF supplied to the power recovery device 24 '.
- the same low-pressure feed LPF is introduced into one pair of chambers 48a arranged symmetrically with respect to each other, and at the same time, the other pair of chambers 48b arranged symmetrically with respect to each other with the central axis 44 interposed therebetween.
- the same high pressure brine HPB is introduced.
- the mixture of the low-pressure brine LPB and the high-pressure brine HPB that have entered the gap between the outer peripheral surface of the other end of the central shaft 44 and the inner peripheral surface 46 b of the bottomed hole 46 a of the rotating member 46 is the outer periphery of the central shaft 44. Along with the rotation of the rotating member 46 on the surface, it functions as a radial dynamic pressure bearing between the outer peripheral surface of the other end of the central shaft 44 and the inner peripheral surface 46b of the bottomed hole 46a of the rotating member 46.
- the low-pressure brine LPB that has entered a gap between the inner surface of the lid 43b of the housing 43 and the one side surface facing the inner surface in the rotating member 46 in the inner space 41 of the case 42a of the housing 43, and
- the mixture of the high-pressure brine HPB and the mixture of the low-pressure feed LPF and the high-pressure feed HPF are rotated on the outer peripheral surface of the other end of the central shaft 44 and the inner surface of the lid 43b and the one side surface of the rotary member 46 are rotated. It functions as a thrust bearing between.
- the mixture of the low-pressure brine LPB and the high-pressure brine HPB entering the gap between the end surface of the other end portion of the central shaft 44 and the bottom surface of the bottomed hole 46 a of the rotating member 46 is the outer periphery of the other end portion of the central shaft 44.
- the rotating member 46 functions as a thrust bearing between the end surface of the other end portion of the central shaft 44 and the bottom surface of the bottomed hole 46 a of the rotating member 46.
- the low pressure feed that has entered the gap between the lower surface of the inner space 41 of the case 42a of the housing 43 and the other side surface of the rotating member 46 in the inner space 41 of the case 42a of the housing 43 facing the bottom surface.
- the mixture of the LPF and the high pressure feed HPF is formed between the lower surface of the internal space 41 of the case 42 a and the other side surface of the rotating member 46 as the rotating member 46 rotates on the outer peripheral surface of the other end portion of the central shaft 44. It functions as a thrust bearing.
Abstract
Description
高濃度原水が維持している高圧力のエネルギーを簡易な構成でありながら高い効率で回収して逆浸透膜に供給される新たな原水の圧力を上昇させ、高圧で逆浸透膜に供給される新たな原水の圧力上昇のために必要な新たな外部エネルギーの量を削減でき、ひいては液体処理装置の運転に必要なエネルギー量、即ち動力、を少なくすることが出来る、液体処理装置の動力回収装置を提供することである。 [Problems to be solved by the invention]
The high-pressure energy maintained by the high-concentration raw water is recovered with high efficiency and the pressure of new raw water supplied to the reverse osmosis membrane is increased with a simple configuration, and the high-pressure raw water is supplied to the reverse osmosis membrane at high pressure. A power recovery device for a liquid processing apparatus that can reduce the amount of new external energy required for increasing the pressure of new raw water, and thus can reduce the amount of energy required for operation of the liquid processing apparatus, that is, the power. Is to provide.
この発明の一実施形態に従った、液体処理装置の動力回収装置は、外部から供給され複数の成分を含む水である原水を圧力上昇ユニットを介し逆浸透膜に送り逆浸透膜において原水から水の一部を抽出する液体処理装置において使用され、逆浸透膜において水の一部が抽出された後の残りの原水の圧力を利用して圧力上昇させた原水を圧力上昇ユニットからの原水に加えて逆浸透膜に送る動力回収装置である。 [Means for solving problems]
According to one embodiment of the present invention, a power recovery device for a liquid processing apparatus sends raw water, which is water supplied from the outside and contains a plurality of components, to a reverse osmosis membrane via a pressure increase unit, and then water from the raw water in the reverse osmosis membrane. Used in a liquid processing apparatus for extracting a part of the raw water, and the raw water whose pressure has been increased by using the pressure of the remaining raw water after the water is partially extracted in the reverse osmosis membrane is added to the raw water from the pressure increasing unit. Power recovery device that feeds the reverse osmosis membrane.
次に、図2乃至図7を参照しながら、第1実施形態の動力回収装置24の構成について説明する。 [First Embodiment]
Next, the configuration of the
次に、図10乃至図14を参照しながら、図2乃至図9を参照しながら前述した第1実施形態の動力回収装置24に代わり、図1を参照しながら前述した一例の液体処理装置において使用可能なこの発明の第2実施形態に従った動力回収装置24´の構成について説明する。 [Second Embodiment]
Next, instead of the
Claims (5)
- 外部から供給され複数の成分を含む水である原水(SW)を圧力上昇ユニット(16)を介し逆浸透膜(18a)に送り逆浸透膜において原水(HPSW)から水の一部(FW)を抽出する液体処理装置において使用され、逆浸透膜において水の一部が抽出された後の残りの原水(HPB)の圧力を利用して圧力上昇させた原水(HPF)を圧力上昇ユニットからの原水(HPSW)に加えて逆浸透膜に送る動力回収装置であって:
内部空間(30,41)を有するハウジング(32,43)と;ハウジングの内部空間に固定され外周面(36b,46c)とハウジングの外部に突出した少なくとも1つの端部とを有した中心軸(34,44)と;そして、ハウジングの内部空間に中心軸の外周面の周りに回転自在に収容され、中心軸の外周面に対面した内周面(36a,46b)と中心軸の半径方向の外方に位置した外周面(36b,46c)とを有し、中心軸の周方向に等間隔に配置され夫々が内周面と外周面との間を延出している複数の通路(36c,46d)を含む回転部材(36,46)と、を備え、
ハウジングの内部空間には、回転部材の外周面に対面し相互に区画された2対1組の少なくとも1組の室(38a,38b;48a,48b)が設けられ、
中心軸には、中心軸の外周面に形成されハウジングの内部空間の少なくとも1組の室に回転部材を介して対向し前記室と同数の2対1組の少なくとも1組の開口(40a,40b:50a,50b)と、少なくとも1組の開口から中心軸中を延出し中心軸の前記少なくとも1つの端部に開口した2対1組の少なくとも1組の通路(42a,42b:52a,52b)と、が形成され、
ハウジングの内部空間の前記1組の室において中心軸を挟んで相互に対称に配置されている一方の1対の室(38a;48a)は、外部から供給される原水(LPF)が導入され導入された原水を前記一方の1対の室中に露出している回転部材の外周面の複数の通路に対し前記外周面の所定の周方向に押し当てて回転部材を回転させるよう構成され、
前記1組の室において中心軸を挟んで相互に対称に配置されている他方の1対の室(38b;48b)は、圧力上昇ユニット(16)と逆浸透膜(18a)との間の原水(HPSW)の通路に接続されており、
中心軸の外周面の前記1組の開口において回転部材を介し前記一方の1対の室(38a;48a)に対向している一方の1対の開口(40a;50a)は中心軸の対応する一方の1対の通路(42a;52a)を介して外部に連通されており、
中心軸の外周面の前記1組の開口において回転部材を介し前記他方の1対の室(38b;48b)に対向している他方の1対の開口(40b;50b)には中心軸の対応する他方の1対の通路(42b;52b)を介して前記残りの原水(HPB)が導入される、
ことを特徴とする液体処理装置の動力回収装置。 Raw water (SW), which is water supplied from the outside and containing a plurality of components, is sent to the reverse osmosis membrane (18a) via the pressure increase unit (16), and part of the water (HPSW) from the raw water (HPSW) in the reverse osmosis membrane. Raw water (HPF) that is used in the liquid processing apparatus to be extracted and is pressure-enhanced using the pressure of the remaining raw water (HPB) after a part of the water is extracted in the reverse osmosis membrane is supplied from the pressure increasing unit. In addition to (HPSW), a power recovery device that sends to a reverse osmosis membrane:
A housing (32, 43) having an internal space (30, 41); a central shaft having an outer peripheral surface (36b, 46c) fixed to the internal space of the housing and at least one end projecting to the outside of the housing ( 34, 44); and an inner peripheral surface (36a, 46b) which is rotatably accommodated around the outer peripheral surface of the central axis in the inner space of the housing and faces the outer peripheral surface of the central axis, and the radial direction of the central axis A plurality of passages (36c, 46c, 36b, 46c) having outer peripheral surfaces (36b, 46c) located on the outer sides and arranged at equal intervals in the circumferential direction of the central axis, each extending between the inner peripheral surface and the outer peripheral surface. A rotating member (36, 46) including 46d),
The interior space of the housing is provided with at least one pair of chambers (38a, 38b; 48a, 48b) which are two-to-one pairs facing the outer peripheral surface of the rotating member and partitioned from each other.
The central axis is formed on the outer peripheral surface of the central axis and faces at least one pair of chambers in the inner space of the housing through a rotating member, and has at least one pair of openings (40a, 40b) of the same number as the chambers. : 50a, 50b) and at least one pair of passages (42a, 42b: 52a, 52b) extending from the at least one set of openings into the central axis and opening at the at least one end of the central axis And formed,
One pair of chambers (38a; 48a) arranged symmetrically with respect to the central axis in the pair of chambers in the internal space of the housing is introduced with the introduction of raw water (LPF) supplied from the outside. Configured to rotate the rotating member by pressing the raw water in a predetermined circumferential direction of the outer peripheral surface against a plurality of passages on the outer peripheral surface of the rotating member exposed in the one pair of chambers,
The other pair of chambers (38b; 48b) disposed symmetrically with respect to the central axis in the pair of chambers is the raw water between the pressure raising unit (16) and the reverse osmosis membrane (18a). (HPSW) is connected to the passage,
One pair of openings (40a; 50a) facing the one pair of chambers (38a; 48a) through the rotating member in the pair of openings on the outer peripheral surface of the central axis corresponds to the central axis. Communicated to the outside through one pair of passages (42a; 52a),
The pair of openings (40b; 50b) facing the other pair of chambers (38b; 48b) through the rotating member in the pair of openings on the outer peripheral surface of the center axis corresponds to the center axis. The remaining raw water (HPB) is introduced through the other pair of passages (42b; 52b).
A power recovery device for a liquid processing apparatus. - 前記中心軸(34)は細長く前記中心軸の長手方向中心線に沿って前記1つの端部とは反対側において前記ハウジング(32)の外部に突出したもう1つの端部を有しており、
前記中心軸(34)の前記一方の1対の通路(42a)は前記中心軸の前記1つの端部に開口し、
前記中心軸の前記他方の1対の通路(42b)は前記中心軸の前記もう1つの端部に開口している、
ことを特徴とする請求項1記載の液体処理装置の動力回収装置。 The central axis (34) is elongated and has another end projecting out of the housing (32) on the opposite side of the central axis along the longitudinal centerline of the central axis;
The one pair of passages (42a) of the central axis (34) open to the one end of the central axis;
The other pair of passages (42b) of the central axis is open to the other end of the central axis;
The power recovery apparatus for a liquid processing apparatus according to claim 1. - 前記中心軸(44)は細長く、前記中心軸の長手方向中心線に沿って前記1つの端部とは反対側に位置し前記ハウジング(43)の内部空間(41)に収容されているもう1つの端部を有している、
ことを特徴とする請求項1記載の液体処理装置の動力回収装置。 The central axis (44) is elongated and is located on the opposite side of the one end along the longitudinal center line of the central axis and is accommodated in the internal space (41) of the housing (43). Has two ends,
The power recovery apparatus for a liquid processing apparatus according to claim 1. - 前記回転部材(46)に連結され前記回転部材とともに回転する出力軸(54a)を有する電動モータ(54)をさらに備えている、ことを特徴とする請求項1記載の液体処理装置の動力回収装置。 The power recovery apparatus for a liquid processing apparatus according to claim 1, further comprising an electric motor (54) connected to the rotating member (46) and having an output shaft (54a) that rotates together with the rotating member. .
- 前記原水(SW)は塩水である、ことを特徴とする請求項1乃至4のいずれか1項に記載の液体処理装置の動力回収装置。 The power recovery apparatus for a liquid processing apparatus according to any one of claims 1 to 4, wherein the raw water (SW) is salt water.
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PCT/JP2010/059220 WO2011151883A1 (en) | 2010-05-31 | 2010-05-31 | Power recovery device of liquid treatment apparatus |
AU2010354672A AU2010354672B2 (en) | 2010-05-31 | 2010-05-31 | Power recovery device of liquid treatment apparatus |
CN2010800658995A CN102822449A (en) | 2010-05-31 | 2010-05-31 | Power recovery device of liquid treatment apparatus |
JP2012518165A JP5337301B2 (en) | 2010-05-31 | 2010-05-31 | Power recovery device for liquid processing equipment |
US13/687,017 US20130094949A1 (en) | 2010-05-31 | 2012-11-28 | Power recovery device of liquid processing apparatus |
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JP4138470B2 (en) * | 2002-12-12 | 2008-08-27 | 日本フイルター株式会社 | Filter |
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JPH01294903A (en) * | 1988-02-26 | 1989-11-28 | Robert A Oklejas | Power recovery pump turbine |
JPH10205301A (en) * | 1997-01-17 | 1998-08-04 | Unyusho Kowan Gijutsu Kenkyusho | Turbine device |
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