WO2019181041A1 - Reverse osmosis treatment method and device - Google Patents
Reverse osmosis treatment method and device Download PDFInfo
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- WO2019181041A1 WO2019181041A1 PCT/JP2018/039490 JP2018039490W WO2019181041A1 WO 2019181041 A1 WO2019181041 A1 WO 2019181041A1 JP 2018039490 W JP2018039490 W JP 2018039490W WO 2019181041 A1 WO2019181041 A1 WO 2019181041A1
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- water
- reverse osmosis
- heat pump
- heat
- osmosis membrane
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- 238000001223 reverse osmosis Methods 0.000 title claims description 38
- 238000000034 method Methods 0.000 title claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims abstract description 13
- 239000012528 membrane Substances 0.000 claims description 27
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 5
- 239000008235 industrial water Substances 0.000 claims description 2
- 239000002349 well water Substances 0.000 claims description 2
- 235000020681 well water Nutrition 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 14
- 239000000377 silicon dioxide Substances 0.000 description 7
- 239000002455 scale inhibitor Substances 0.000 description 5
- 239000011575 calcium Substances 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
Images
Classifications
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- 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
- B01D61/04—Feed pretreatment
-
- 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
- B01D61/06—Energy recovery
-
- 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
- B01D61/08—Apparatus therefor
-
- 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
Definitions
- the present invention relates to a reverse osmosis treatment method and apparatus for treating water using a reverse osmosis membrane device.
- the water supply temperature is heated to about 25 ° C. in order to maintain the amount of treated water.
- the temperature of water is increased to lower the viscosity, the flux of the RO device increases.
- the temperature of water is increased to increase the silica saturation solubility, the RO device recovery rate is improved.
- Patent Document 1 in a reverse osmosis treatment method in which water to be treated (raw water) is heated by a heat pump and then subjected to membrane separation treatment by a reverse osmosis membrane device, the reverse osmosis membrane device is used as at least part of the heat source fluid of the heat pump.
- a reverse osmosis treatment method using concentrated water is described.
- the present invention aims to reduce the heating cost by heating the water supply to the RO device with a heat pump using RO concentrated water as a heat source, and to effectively use water resources.
- concentrated water from another reverse osmosis membrane device is used as part of the heat source fluid of the heat pump.
- the reverse osmosis treatment device of the present invention is a reverse osmosis treatment device that heats raw water with a heat pump and then performs membrane separation treatment with a reverse osmosis membrane device.
- the concentrated water of the reverse osmosis membrane device is used as at least part of the heat source fluid of the heat pump. It is characterized by comprising means for passing water and means for supplying at least a part of the concentrated water of the reverse osmosis membrane device to the cooling tower as make-up water.
- the heating cost can be reduced by heating the water supply to the RO device with the heat pump using the RO concentrated water as a heat source.
- the water resources can be effectively used by supplying the RO concentrated water to the cooling tower.
- the RO concentrated water is supplied to the cooling tower after heat exchange with a heat pump (that is, after cooling), the load on the cooling tower is not increased and the thermal efficiency is good.
- the concentrated water of other reverse osmosis membrane devices can also be used as a water resource.
- FIG. 1 is a block diagram of a reverse osmosis treatment apparatus according to an embodiment.
- the raw water to be RO-treated (in this embodiment, clean water) is supplied from the pipe 1 to the heat exchanger 2, heated, and then supplied from the pipe 3 to the heater (electric heater, steam heat exchanger, etc.) 4. After being further heated, it is supplied to the RO device 6 through the pipe 5.
- the permeated water of the RO device 6 is taken out from the pipe 7 as treated water, and the concentrated water flows out to the pipe 8 and is used as a heat source fluid of the heat pump 20.
- the concentrated water from the pipe 8 is stored in the concentrated water tank 9.
- Concentrated water from a reverse osmosis membrane device installed in a system other than the reverse osmosis membrane device 6 is also introduced into the concentrated water tank 9 via a pipe 10.
- the concentrated water in the tank 9 is sent to the evaporator 21 of the heat pump 20 through the pump 11 and the pipe 12.
- the medium water heated by the condenser 23 of the heat pump 20 (water as a heat transfer medium) is circulated through the heat source fluid flow path of the heat exchanger 2.
- the heat pump 20 compresses the heat medium such as alternative CFC from the evaporator 21 by the compressor 22 and introduces it into the condenser 23, and introduces the heat medium from the condenser 23 into the evaporator 21 through the expansion valve 24. It is configured as follows.
- the medium water from the heat exchanger 2 is introduced into the condenser 23 via the pipe 25, the tank 28 and the pump 27, and the medium water heated by the condenser 23 is sent to the heat exchanger 2 via the pipe 26. .
- the concentrated water in the tank 9 is introduced from the pipe 12 into the heat source fluid flow path of the evaporator 21.
- the concentrated water cooled by heat exchange is sent to the cooling tower 14 via the pipe 13 as makeup water.
- Clean water is also sent to the cooling tower 14 as makeup water through the pipe 15.
- the makeup water is supplied to the cooling tower 4 through a ball tap (not shown).
- the following measures i), ii) or iii) are taken to prevent scale and slime in the evaporator 21, the RO device 6, and the pipes 8, 12, and 13.
- the pH of the raw water is adjusted by the RO device 6 and the heat pump evaporator 21 so that silica scale does not precipitate.
- the pH is set to 9 or more (for example, 9 to 11) under the condition that the Ca hardness of the raw water is 5 mg / L or less.
- the pH of the raw water is set to 6 or less (for example, 4 to 6).
- the pH of the raw water may be 6 or less (for example, 4 to 6), or a water softener may be provided in front of the RO membrane to remove the hardness component.
- a scale inhibitor for calcium scale may be added to raw water, and in that case, the Langeria index may exceed zero.
- the Langeria index may be 0.5 or less by using the organic polymer scale inhibitor.
- the above embodiment is an example of the present invention, and the present invention may be other than the above.
- well water or industrial water other than tap water may be used as raw water.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Nanotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Raw water is supplied from piping 1, heated with a heat exchanger 2 and a heater 4, and then supplied to a RO device 6. The water that has passed through the RO device 6 is taken from the piping 7 as treated water, and concentrated water is passed via piping 8 and a tank 9 to the evaporator 21 of a heat pump 20 as a heat source fluid for the heat pump 20. Medium water that was heated by the condenser 23 of the heat pump 20 is recirculated to a heat source fluid flow channel of the heat exchanger 2. The condensed water that was heated by the evaporator 21 is supplied to a cooling tower 14 as resupply water.
Description
本発明は、逆浸透膜装置を用いて水を処理する逆浸透処理方法及び装置に関する。
The present invention relates to a reverse osmosis treatment method and apparatus for treating water using a reverse osmosis membrane device.
逆浸透膜装置（以下、ＲＯ装置ということがある。）にあっては、処理水量維持の為、給水温度を２５℃程度に加温している。水の温度を高くして粘度を低下させると、ＲＯ装置のフラックスが多くなる。水の温度を高くしてシリカ飽和溶解度を大きくすると、ＲＯ装置の回収率が向上する。
In the reverse osmosis membrane device (hereinafter sometimes referred to as RO device), the water supply temperature is heated to about 25 ° C. in order to maintain the amount of treated water. When the temperature of water is increased to lower the viscosity, the flux of the RO device increases. When the temperature of water is increased to increase the silica saturation solubility, the RO device recovery rate is improved.
ＲＯ装置の給水を、蒸気、温水、電気ヒーター等によって加熱する場合、加熱コストが高い。給水加熱に投入したエネルギーは、昇温した濃縮水と一緒に廃棄されることなり、エネルギーロスとなる。
When heating the RO device water supply with steam, hot water, electric heater, etc., the heating cost is high. The energy input to the feed water heating is discarded together with the concentrated water whose temperature has been raised, resulting in an energy loss.
特許文献１には、被処理水（原水）をヒートポンプで加熱した後、逆浸透膜装置で膜分離処理する逆浸透処理方法において、該ヒートポンプの熱源流体の少なくとも一部として該逆浸透膜装置の濃縮水を用いる逆浸透処理方法が記載されている。
In Patent Document 1, in a reverse osmosis treatment method in which water to be treated (raw water) is heated by a heat pump and then subjected to membrane separation treatment by a reverse osmosis membrane device, the reverse osmosis membrane device is used as at least part of the heat source fluid of the heat pump. A reverse osmosis treatment method using concentrated water is described.
本発明は、ＲＯ濃縮水を熱源としたヒートポンプでＲＯ装置への給水を加熱することにより加熱コストを低減すると共に、水資源の有効利用を図ることを目的とする。
The present invention aims to reduce the heating cost by heating the water supply to the RO device with a heat pump using RO concentrated water as a heat source, and to effectively use water resources.
本発明の逆浸透処理方法は、原水をヒートポンプで加熱した後、逆浸透膜装置で膜分離処理する逆浸透処理方法において、該ヒートポンプの熱源流体の少なくとも一部として該逆浸透膜装置の濃縮水を用い、該逆浸透膜装置の濃縮水の少なくとも一部を冷却塔に補給水として供給することを特徴とする。
The reverse osmosis treatment method of the present invention is a reverse osmosis treatment method in which raw water is heated with a heat pump and then subjected to membrane separation treatment with a reverse osmosis membrane device. In the reverse osmosis treatment method, the concentrated water of the reverse osmosis membrane device is used as at least part of the heat source fluid of the heat pump. And at least a part of the concentrated water of the reverse osmosis membrane device is supplied to the cooling tower as make-up water.
本発明の一態様では、前記ヒートポンプの熱源流体の一部として、他の逆浸透膜装置の濃縮水を用いる。
In one aspect of the present invention, concentrated water from another reverse osmosis membrane device is used as part of the heat source fluid of the heat pump.
本発明の逆浸透処理装置は、原水をヒートポンプで加熱した後、逆浸透膜装置で膜分離処理する逆浸透処理装置において、該ヒートポンプの熱源流体の少なくとも一部として該逆浸透膜装置の濃縮水を通水する手段と、該逆浸透膜装置の濃縮水の少なくとも一部を冷却塔に補給水として供給する手段とを備えたことを特徴とする。
The reverse osmosis treatment device of the present invention is a reverse osmosis treatment device that heats raw water with a heat pump and then performs membrane separation treatment with a reverse osmosis membrane device. In the reverse osmosis treatment device, the concentrated water of the reverse osmosis membrane device is used as at least part of the heat source fluid of the heat pump. It is characterized by comprising means for passing water and means for supplying at least a part of the concentrated water of the reverse osmosis membrane device to the cooling tower as make-up water.
本発明によると、ＲＯ濃縮水を熱源としたヒートポンプでＲＯ装置への給水を加熱することにより、加熱コストを低減することができる。また、ＲＯ濃縮水を冷却塔に供給することにより、水資源の有効利用を図ることができる。また、ＲＯ濃縮水をヒートポンプで熱交換した後に（すなわち冷ました後で）冷却塔に投入するため、冷却塔の負荷を高めることはなく、熱効率が良い。
According to the present invention, the heating cost can be reduced by heating the water supply to the RO device with the heat pump using the RO concentrated water as a heat source. Moreover, the water resources can be effectively used by supplying the RO concentrated water to the cooling tower. In addition, since the RO concentrated water is supplied to the cooling tower after heat exchange with a heat pump (that is, after cooling), the load on the cooling tower is not increased and the thermal efficiency is good.
本発明の一態様によると、他の逆浸透膜装置の濃縮水も水資源として利用することができる。
According to one aspect of the present invention, the concentrated water of other reverse osmosis membrane devices can also be used as a water resource.
以下、図１を参照して実施の形態について説明する。
Hereinafter, an embodiment will be described with reference to FIG.
ＲＯ処理される原水（この実施の形態では上水）は、配管１から熱交換器２に供給され、加熱された後、配管３から加熱器（電気ヒータや蒸気熱交換器など）４に供給され、さらに加熱された後、配管５を介してＲＯ装置６に供給される。ＲＯ装置６の透過水は配管７から処理水として取り出され、濃縮水は配管８へ流出し、ヒートポンプ２０の熱源流体として利用される。
The raw water to be RO-treated (in this embodiment, clean water) is supplied from the pipe 1 to the heat exchanger 2, heated, and then supplied from the pipe 3 to the heater (electric heater, steam heat exchanger, etc.) 4. After being further heated, it is supplied to the RO device 6 through the pipe 5. The permeated water of the RO device 6 is taken out from the pipe 7 as treated water, and the concentrated water flows out to the pipe 8 and is used as a heat source fluid of the heat pump 20.
この実施の形態では、配管８からの濃縮水は、濃縮水タンク９に貯留される。この濃縮水タンク９には、逆浸透膜装置６以外の他の系統に設置された逆浸透膜装置の濃縮水も配管１０を介して導入される。
In this embodiment, the concentrated water from the pipe 8 is stored in the concentrated water tank 9. Concentrated water from a reverse osmosis membrane device installed in a system other than the reverse osmosis membrane device 6 is also introduced into the concentrated water tank 9 via a pipe 10.
タンク９内の濃縮水は、ポンプ１１及び配管１２を介してヒートポンプ２０の蒸発器２１に送水される。
The concentrated water in the tank 9 is sent to the evaporator 21 of the heat pump 20 through the pump 11 and the pipe 12.
熱交換器２の熱源流体流路には、ヒートポンプ２０の凝縮器２３によって加熱された媒体水（伝熱媒体としての水）が循環流通される。
The medium water heated by the condenser 23 of the heat pump 20 (water as a heat transfer medium) is circulated through the heat source fluid flow path of the heat exchanger 2.
ヒートポンプ２０は、蒸発器２１からの代替フロン等の熱媒体を圧縮機２２で圧縮して凝縮器２３に導入し、凝縮器２３からの熱媒体を膨張弁２４を介して蒸発器２１に導入するように構成されている。
The heat pump 20 compresses the heat medium such as alternative CFC from the evaporator 21 by the compressor 22 and introduces it into the condenser 23, and introduces the heat medium from the condenser 23 into the evaporator 21 through the expansion valve 24. It is configured as follows.
凝縮器２３に熱交換器２からの媒体水が配管２５、タンク２８及びポンプ２７を介して導入され、凝縮器２３で加熱された媒体水が配管２６を介して熱交換器２に送水される。
The medium water from the heat exchanger 2 is introduced into the condenser 23 via the pipe 25, the tank 28 and the pump 27, and the medium water heated by the condenser 23 is sent to the heat exchanger 2 via the pipe 26. .
前記の通り、蒸発器２１の熱源流体流路に配管１２からタンク９内の濃縮水が導入される。熱交換により降温した濃縮水は、配管１３を介して冷却塔１４へ補給水として送水される。冷却塔１４へは、上水も配管１５を介して補給水として送水される。補給水はボールタップ（図示略）を介して冷却塔４に供給される。
As described above, the concentrated water in the tank 9 is introduced from the pipe 12 into the heat source fluid flow path of the evaporator 21. The concentrated water cooled by heat exchange is sent to the cooling tower 14 via the pipe 13 as makeup water. Clean water is also sent to the cooling tower 14 as makeup water through the pipe 15. The makeup water is supplied to the cooling tower 4 through a ball tap (not shown).
ＲＯ装置６の濃縮水のスケール成分濃度や有機物濃度が原水よりも高いため、ヒートポンプ２０の蒸発器２１や配管８，１２，１３でスケールやスライムが発生するおそれが高いので、これを防止ないし抑制（以下、防止という。）する必要がある。また、ＲＯ装置６においてもスケールやスライムが発生することを防止する必要がある。
Since the scale component concentration and organic matter concentration of the concentrated water of the RO device 6 are higher than the raw water, there is a high possibility that scale and slime are generated in the evaporator 21 and the pipes 8, 12, and 13 of the heat pump 20. (Hereinafter referred to as prevention). Further, it is necessary to prevent the scale and slime from being generated in the RO device 6.
そこで、この実施の形態では、蒸発器２１や、ＲＯ装置６、配管８，１２，１３におけるスケール、スライム防止のために次のｉ），ii）又はiii）の対策を行う。
Therefore, in this embodiment, the following measures i), ii) or iii) are taken to prevent scale and slime in the evaporator 21, the RO device 6, and the pipes 8, 12, and 13.
i） 蒸発器２１の熱源流体側を流れる濃縮水のシリカ濃度がシリカスケール析出濃度を超えない様に、及び／又は、ランゲリア指数が０以下となるように、ＲＯ回収率及び原水温度の一方又は双方を調整する。
i) One of the RO recovery rate and the raw water temperature so that the silica concentration of the concentrated water flowing on the heat source fluid side of the evaporator 21 does not exceed the silica scale precipitation concentration and / or the Langeria index is 0 or less. Adjust both.
ii） ＲＯ装置６およびヒートポンプ蒸発器２１でシリカスケールが析出しない様に原水のｐＨを調整する。具体的には、原水のＣａ硬度が５ｍｇ／Ｌ以下の条件でｐＨを９以上（例えば、９～１１）とする。又は、原水のｐＨを６以下（例えば、４～６）とする。高ｐＨでシリカをイオン化させることにより、ゲル化を抑制し、スケール析出を抑制することができる。また、原水を低ｐＨとすることにより、シリカの析出速度を低下させてシリカスケールを抑制することができる。
ii) The pH of the raw water is adjusted by the RO device 6 and the heat pump evaporator 21 so that silica scale does not precipitate. Specifically, the pH is set to 9 or more (for example, 9 to 11) under the condition that the Ca hardness of the raw water is 5 mg / L or less. Alternatively, the pH of the raw water is set to 6 or less (for example, 4 to 6). By ionizing silica at a high pH, gelation can be suppressed and scale deposition can be suppressed. Moreover, by setting the raw water to a low pH, the silica deposition rate can be reduced to suppress the silica scale.
iii） ＲＯ装置６およびヒートポンプ蒸発器２１でスケール、スライムが析出しない様に原水に薬品（スケール防止剤やスライム防止剤など）を添加する。スケール防止剤やスライム防止剤としては、特に制限はなく、各種のものを用いることができる。
iii) Add chemicals (such as scale inhibitor and anti-slime agent) to the raw water so that scale and slime do not precipitate in RO device 6 and heat pump evaporator 21. There is no restriction | limiting in particular as a scale inhibitor or a slime inhibitor, Various things can be used.
ランゲリア指数を０以下とするには、原水のｐＨを６以下（例えば、４～６）とするか、又は、ＲＯ膜の前段に軟水器を設けて硬度成分を除去するようにしても良い。なお、カルシウムスケール用のスケール防止剤を原水に添加しても良く、その場合は、ランゲリア指数は０を超えても良い。例えば、スケール防止剤の性能にもよるが、有機高分子スケール防止剤を利用することにより、ランゲリア指数を０．５以下となるように制御することが可能となる。
In order to make the Langeria index 0 or less, the pH of the raw water may be 6 or less (for example, 4 to 6), or a water softener may be provided in front of the RO membrane to remove the hardness component. In addition, a scale inhibitor for calcium scale may be added to raw water, and in that case, the Langeria index may exceed zero. For example, depending on the performance of the scale inhibitor, it is possible to control the Langeria index to be 0.5 or less by using the organic polymer scale inhibitor.
上記実施の形態は本発明の一例であり、本発明は上記以外の形態とされてもよい。本発明では、原水として、上水以外の井水や工業用水などを用いてもよい。
The above embodiment is an example of the present invention, and the present invention may be other than the above. In the present invention, well water or industrial water other than tap water may be used as raw water.
本発明を特定の態様を用いて詳細に説明したが、本発明の意図と範囲を離れることなく様々な変更が可能であることは当業者に明らかである。
本出願は、２０１８年３月２０日付で出願された日本特許出願２０１８－０５３２３７に基づいており、その全体が引用により援用される。 Although the present invention has been described in detail using specific embodiments, it will be apparent to those skilled in the art that various modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2018-053237 filed on Mar. 20, 2018, which is incorporated by reference in its entirety.
本出願は、２０１８年３月２０日付で出願された日本特許出願２０１８－０５３２３７に基づいており、その全体が引用により援用される。 Although the present invention has been described in detail using specific embodiments, it will be apparent to those skilled in the art that various modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2018-053237 filed on Mar. 20, 2018, which is incorporated by reference in its entirety.
２ 熱交換器
６ ＲＯ装置
１４ 冷却塔
２０ ヒートポンプ
２１ 蒸発器
２２ 圧縮機
２３ 凝縮器
２４ 膨張弁 2Heat Exchanger 6 RO Device 14 Cooling Tower 20 Heat Pump 21 Evaporator 22 Compressor 23 Condenser 24 Expansion Valve
６ ＲＯ装置
１４ 冷却塔
２０ ヒートポンプ
２１ 蒸発器
２２ 圧縮機
２３ 凝縮器
２４ 膨張弁 2
Claims (4)
- 原水をヒートポンプで加熱した後、逆浸透膜装置で膜分離処理する逆浸透処理方法において、
該ヒートポンプの熱源流体の少なくとも一部として該逆浸透膜装置の濃縮水を用い、
該逆浸透膜装置の濃縮水の少なくとも一部を冷却塔に補給水として供給することを特徴とする逆浸透処理方法。 In the reverse osmosis treatment method in which the raw water is heated with a heat pump and then subjected to membrane separation treatment with a reverse osmosis membrane device,
Using the concentrated water of the reverse osmosis membrane device as at least part of the heat source fluid of the heat pump,
A reverse osmosis treatment method, wherein at least a part of the concentrated water of the reverse osmosis membrane device is supplied to a cooling tower as makeup water. - 請求項１において、前記ヒートポンプの熱源流体の一部として、他の逆浸透膜装置の濃縮水を用いることを特徴とする逆浸透処理方法。 2. The reverse osmosis treatment method according to claim 1, wherein the concentrated water of another reverse osmosis membrane device is used as a part of a heat source fluid of the heat pump.
- 請求項１又は２において、原水は、上水、井水又は工業用水であることを特徴とする逆浸透処理方法。 3. The reverse osmosis treatment method according to claim 1, wherein the raw water is clean water, well water or industrial water.
- 原水をヒートポンプで加熱した後、逆浸透膜装置で膜分離処理する逆浸透処理装置において、
該ヒートポンプの熱源流体の少なくとも一部として該逆浸透膜装置の濃縮水を通水する手段と、
該逆浸透膜装置の濃縮水の少なくとも一部を冷却塔に補給水として供給する手段とを備えたことを特徴とする逆浸透処理装置。 In the reverse osmosis treatment device that performs membrane separation treatment with the reverse osmosis membrane device after heating the raw water with a heat pump,
Means for passing the concentrated water of the reverse osmosis membrane device as at least part of the heat source fluid of the heat pump;
A reverse osmosis treatment device, comprising: means for supplying at least a part of the concentrated water of the reverse osmosis membrane device to the cooling tower as makeup water.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2018-053237 | 2018-03-20 | ||
| JP2018053237A JP6590016B2 (en) | 2018-03-20 | 2018-03-20 | Reverse osmosis processing method and apparatus |
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| Publication Number | Publication Date |
|---|---|
| WO2019181041A1 true WO2019181041A1 (en) | 2019-09-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2018/039490 WO2019181041A1 (en) | 2018-03-20 | 2018-10-24 | Reverse osmosis treatment method and device |
Country Status (2)
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| JP (1) | JP6590016B2 (en) |
| WO (1) | WO2019181041A1 (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS634808A (en) * | 1986-06-24 | 1988-01-09 | Takuma Co Ltd | Reverse-osmosis membrane device system |
| JP2002310595A (en) * | 2001-04-12 | 2002-10-23 | Ebara Corp | Cooler |
| JP2009039599A (en) * | 2007-08-06 | 2009-02-26 | Kurita Water Ind Ltd | Water treatment system |
| JP2012091118A (en) * | 2010-10-27 | 2012-05-17 | Japan Organo Co Ltd | Water treatment system and water treatment method |
| JP2014030777A (en) * | 2012-08-01 | 2014-02-20 | Jfe Engineering Corp | Method and device for processing wastewater from incineration plant |
| JP2016190224A (en) * | 2015-03-31 | 2016-11-10 | 栗田工業株式会社 | Water treatment method and equipment |
-
2018
- 2018-03-20 JP JP2018053237A patent/JP6590016B2/en active Active
- 2018-10-24 WO PCT/JP2018/039490 patent/WO2019181041A1/en active Application Filing
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS634808A (en) * | 1986-06-24 | 1988-01-09 | Takuma Co Ltd | Reverse-osmosis membrane device system |
| JP2002310595A (en) * | 2001-04-12 | 2002-10-23 | Ebara Corp | Cooler |
| JP2009039599A (en) * | 2007-08-06 | 2009-02-26 | Kurita Water Ind Ltd | Water treatment system |
| JP2012091118A (en) * | 2010-10-27 | 2012-05-17 | Japan Organo Co Ltd | Water treatment system and water treatment method |
| JP2014030777A (en) * | 2012-08-01 | 2014-02-20 | Jfe Engineering Corp | Method and device for processing wastewater from incineration plant |
| JP2016190224A (en) * | 2015-03-31 | 2016-11-10 | 栗田工業株式会社 | Water treatment method and equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JP6590016B2 (en) | 2019-10-16 |
| JP2019162600A (en) | 2019-09-26 |
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