JPH02164500A - Water purifying treatment apparatus - Google Patents
Water purifying treatment apparatusInfo
- Publication number
- JPH02164500A JPH02164500A JP63320136A JP32013688A JPH02164500A JP H02164500 A JPH02164500 A JP H02164500A JP 63320136 A JP63320136 A JP 63320136A JP 32013688 A JP32013688 A JP 32013688A JP H02164500 A JPH02164500 A JP H02164500A
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- reverse osmosis
- immobilized
- raw water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 98
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 24
- 150000002500 ions Chemical class 0.000 claims abstract description 15
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000460 chlorine Substances 0.000 claims abstract description 14
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 14
- 230000003647 oxidation Effects 0.000 claims abstract description 14
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000012528 membrane Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 10
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000003456 ion exchange resin Substances 0.000 claims abstract description 9
- 229920003303 ion-exchange polymer Polymers 0.000 claims abstract description 9
- 230000001546 nitrifying effect Effects 0.000 claims abstract description 8
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 6
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 6
- 238000009826 distribution Methods 0.000 claims abstract description 6
- 239000004571 lime Substances 0.000 claims abstract description 6
- 238000004062 sedimentation Methods 0.000 claims abstract description 6
- 239000006228 supernatant Substances 0.000 claims abstract description 6
- 238000002347 injection Methods 0.000 claims abstract description 4
- 239000007924 injection Substances 0.000 claims abstract description 4
- 238000000746 purification Methods 0.000 claims description 22
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- 241000894006 Bacteria Species 0.000 claims description 11
- 238000002242 deionisation method Methods 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 6
- 229920005989 resin Polymers 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 4
- 239000002250 absorbent Substances 0.000 claims description 3
- 230000002745 absorbent Effects 0.000 claims description 3
- 239000000758 substrate Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 13
- 239000000126 substance Substances 0.000 abstract description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 8
- 230000008569 process Effects 0.000 abstract description 6
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 5
- 238000005406 washing Methods 0.000 abstract description 5
- 229910001873 dinitrogen Inorganic materials 0.000 abstract description 4
- 239000008399 tap water Substances 0.000 abstract description 4
- 235000020679 tap water Nutrition 0.000 abstract description 4
- 230000008859 change Effects 0.000 abstract description 3
- 230000006866 deterioration Effects 0.000 abstract description 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 abstract 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 abstract 1
- 230000001580 bacterial effect Effects 0.000 abstract 1
- 230000010485 coping Effects 0.000 abstract 1
- 239000004576 sand Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 239000005416 organic matter Substances 0.000 description 9
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910002651 NO3 Inorganic materials 0.000 description 3
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- -1 nitrate ions Chemical class 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000005446 dissolved organic matter Substances 0.000 description 2
- 229910001410 inorganic ion Inorganic materials 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000001651 autotrophic effect Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
Abstract
Description
【発明の詳細な説明】
A、産業上の利用分野
本発明は、高度浄化処理のできる浄水処理装置に関する
。DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a water purification treatment device capable of high-level purification treatment.
B1発明の概要
本発明の浄水処理装置は、固定床型生物酸化池及び高吸
水性樹脂に硝化菌を固定化した固定化槽で原水中の有機
物の除去及びアンモニア性窒素の硝化を行った後、通常
の急速撹拌、沈澱、ろ過よりなる浄水プロセスを経て濁
質の除去を行い、その後、逆浸透装置を透過させて、溶
解性有機物及び無機イオンの除去を行い、塩素殺菌して
配水池より配水し、一方、逆浸透装置における非透過濃
縮水をイオン交換樹脂により脱イオン化して原水に返送
すると共に、イオン交換樹脂に吸着したイオンを洗浄し
、洗浄した液に石灰を添加して重金属イオンを共沈スラ
ッジと、こ除去し、その上澄水を高吸水性樹脂に脱窒菌
を固定化した固定化脱窒槽に入れ、メタノールを供給し
て硝酸イオンを窒素ガスに変換したのち放流するように
したものである。B1 Overview of the Invention The water purification device of the present invention removes organic matter from raw water and nitrifies ammonia nitrogen using a fixed-bed biological oxidation pond and an immobilization tank in which nitrifying bacteria are immobilized on superabsorbent resin. The water undergoes a normal water purification process consisting of rapid stirring, sedimentation, and filtration to remove suspended solids, and then passes through a reverse osmosis device to remove dissolved organic matter and inorganic ions, sterilizes it with chlorine, and discharges it from the distribution reservoir. On the other hand, the non-permeated concentrated water in the reverse osmosis equipment is deionized with an ion exchange resin and returned to the raw water, and the ions adsorbed on the ion exchange resin are washed, and lime is added to the washed liquid to remove heavy metal ions. Co-precipitated sludge is removed, and the supernatant water is placed in a denitrification tank with denitrification bacteria immobilized on superabsorbent resin, and methanol is supplied to convert nitrate ions into nitrogen gas before being discharged. This is what I did.
C1従来の技術
我が国においては、水道の需要が年々増加しているが、
水の供給能力に限界があり、良質の水源が得難くなって
いる。そのため河川の表流水を水源とするところが多く
なっており、異臭味やトリハロメタン生成などの問題が
生じている。一方、安全で美味い水のニーズが高まって
おり、高度な浄水処理が要求されている。C1 Conventional technology In Japan, the demand for water supply is increasing year by year.
Water supply capacity is limited, making it difficult to obtain high-quality water sources. For this reason, many places use river surface water as their water source, causing problems such as off-flavors and trihalomethane formation. On the other hand, the need for safe and delicious water is increasing, and advanced water purification treatment is required.
現在の浄水処理方法は水中の濁質の除去と殺菌が主体で
あって、溶解物の除去にはあまり有効ではない。そのた
め異臭味やトリハロメタン生成のような溶解性有機物に
起因する問題か生じている。Current water purification methods mainly involve removing suspended solids and sterilizing water, and are not very effective in removing dissolved substances. This has resulted in problems caused by soluble organic matter, such as off-flavors and trihalomethane formation.
水の富栄養化により原水のアンモニア性窒素濃度が上昇
すると、塩素消費量が増加し、トリハロメタン生成潰が
増加するという間型か生じる。現在の一般的な浄水処理
プロセスは第2図のようになっているが、原水の水質が
悪い場合には高度処理を行う必要がある。When the ammoniacal nitrogen concentration of raw water increases due to water eutrophication, chlorine consumption increases and trihalomethane production increases. The current general water purification process is shown in Figure 2, but if the quality of the raw water is poor, advanced treatment is required.
る。Ru.
現在、高度処理法として次のような方法がある。Currently, there are the following advanced processing methods.
溶解性有機物の除去には生物酸化と活性炭吸着、異臭味
や色度の除去殺菌にはオゾン処理が有効である。また、
溶解性無機物の除去にはイオン交換法、溶解性物質(無
機物+有機物)の除去には逆浸透法がある。Biological oxidation and activated carbon adsorption are effective for removing soluble organic matter, and ozone treatment is effective for removing off-flavors, tastes, and sterilization. Also,
There is an ion exchange method for removing soluble inorganic substances, and a reverse osmosis method for removing soluble substances (inorganic substances + organic substances).
D9発明が解決しようとする課題
生物酸化は6機物の除去だけでなく、アンモニアを硝化
し塩素消費量を減少させる効果があるが、水温低下時に
浄化能力、特に硝化能力が低下する欠点がある。また、
オゾン処理、活性炭吸着、イオン交換法は高価となる。D9 Problems to be solved by the invention Biological oxidation has the effect of not only removing six organic substances, but also nitrifying ammonia and reducing chlorine consumption, but it has the disadvantage that the purification ability, especially the nitrification ability, decreases when the water temperature drops. . Also,
Ozone treatment, activated carbon adsorption, and ion exchange methods are expensive.
逆浸透法は溶解性物質の除去に有効であり、将来有望な
方法であるが、大量に発生する濃縮水の処理に問題があ
る。このように何れの方法も一長一短があり、単独で採
用しても処理水質の向上には限界がある。Reverse osmosis is effective in removing soluble substances and is a promising method for the future, but there are problems in processing concentrated water that is generated in large quantities. As described above, each method has its advantages and disadvantages, and there is a limit to the improvement in treated water quality even if adopted alone.
本発明は、従来の技術の有するこのような問題点に鑑み
てなされたものであり、その目的とするところは、水道
原水水質の悪化に対して対応可能な浄水処理装置を提供
することにある。The present invention has been made in view of the above-mentioned problems of the conventional technology, and its purpose is to provide a water purification device that can cope with deterioration in the quality of raw water from tap water. .
61課題を解決するための手段
本発明の浄水処理装置は、水道原水が導入される沈砂池
と、この沈砂池の水が導入される活性汚泥を固定化した
固定床型生物酸化池と、この生物酸化池の処理水が導入
される高吸水性樹脂に硝化菌を固定化した固定化硝化槽
と、この固定化硝化槽の処理水が導入される急速撹拌池
と、この急速撹拌池の撹拌された水が導入される沈澱池
と、この沈澱池の水が導入されるろ通油と、このろ通油
の水が導入される逆浸透装置と、この逆浸透装置の逆浸
透膜透過水が導入される配水池と、前記逆浸透膜透過水
に塩素を注入する塩素注入装置と、前記逆浸透膜非透過
濃縮水のイオンを除去し水道原水中に返送するイオン交
換樹脂を用いた脱イオン装置と、前記イオン交換樹脂を
洗浄した液に石灰を加える洗浄液槽と、この洗浄液槽の
上澄水に固定化脱窒菌を入れメタノールを基質として供
給し脱窒して放流する固定化脱窒槽とよりなるものであ
る。61 Means for Solving the Problems The water purification treatment apparatus of the present invention comprises: a settling basin into which raw water is introduced; a fixed bed type biological oxidation pond in which activated sludge is immobilized into which water from the settling basin is introduced; An immobilized nitrification tank in which nitrifying bacteria are immobilized on superabsorbent resin into which the treated water from the biological oxidation pond is introduced, a rapid stirring pond into which the treated water from this immobilized nitrification tank is introduced, and stirring in this rapid stirring pond. A sedimentation tank into which water is introduced, a filtered oil into which water from the settling tank is introduced, a reverse osmosis device into which water from this filtered oil is introduced, and water permeated through the reverse osmosis membrane of this reverse osmosis device. A water distribution reservoir in which a an ion device, a cleaning liquid tank in which lime is added to the liquid used to wash the ion exchange resin, and an immobilized denitrification tank in which immobilized denitrifying bacteria are put in the supernatant water of the cleaning liquid tank, methanol is supplied as a substrate, the denitrification is performed, and the water is discharged. It is more than that.
F1作用
水道原水は沈砂池で粗大濁質が除去された後、生物酸化
池で好気性微生物による有機物が除去され、次で固定化
硝化槽においてアンモニアの硝化が行われる。After coarse turbidity is removed from F1 action water raw water in a settling pond, organic matter is removed by aerobic microorganisms in a biological oxidation pond, and then ammonia is nitrified in a fixation nitrification tank.
この水は急速撹拌池、沈澱池、ろ通油よりなる通常の浄
水プロセスにより濁質が除去される。This water undergoes a normal water purification process consisting of a rapid stirring pond, settling basin, and filtered oil to remove suspended matter.
この水は逆浸透装置の逆浸透膜を通って溶解性有機物及
びイオンが除去され、塩素殺菌されて配水池に入る。This water passes through the reverse osmosis membrane of the reverse osmosis device, removes dissolved organic matter and ions, and is sterilized with chlorine before entering the water distribution reservoir.
逆浸透膜非透過の濃縮水は脱イオン装置によりイオンが
除去された後水道原水中に返送されて再び沈砂池に入り
、前記浄水処理が行われる。After ions are removed from the concentrated water that has not passed through the reverse osmosis membrane, it is returned to the raw water of the tap water and enters the settling basin again, where the water purification treatment is performed.
脱イオン装置のイオン交換樹脂が飽和して脱イオン能力
が低下した場合洗浄し、その洗浄液は洗浄液槽で石灰が
加えられ重金属イオンが共沈する。When the ion exchange resin in the deionization device becomes saturated and its deionization ability decreases, it is washed, and lime is added to the washing liquid in the washing liquid tank to co-precipitate heavy metal ions.
その上澄水は固定化脱窒槽で濃縮硝酸イオンを窒素ガス
に変化させた後放流される。The supernatant water is discharged after converting concentrated nitrate ions into nitrogen gas in a fixed denitrification tank.
G、実施例 実施例について第1図を参照して説明する。G. Example An embodiment will be described with reference to FIG.
水道原水は沈砂池■こおいて粗大濁質が除去され、生物
酸化池2に入る。生物酸化池2は固定床に好気性微生物
(汚性汚泥)を固定化したもので、エアレージタンを行
って微生物による有機物の除去と活性汚泥中の硝化菌に
よりアンモニアの硝化が行われる。The raw water from the water supply is passed through a settling pond (2) to remove coarse turbidity, and then enters the biological oxidation pond (2). The biological oxidation pond 2 has aerobic microorganisms (poor sludge) immobilized on a fixed bed, and aeration is performed to remove organic matter by the microorganisms and nitrify ammonia by nitrifying bacteria in the activated sludge.
次に固定化硝化槽3においてアンモニアの硝化を行う。Next, ammonia is nitrified in the immobilization nitrification tank 3.
固定化硝化槽3はアンモニアを主体とした培地で選択培
養された硝化菌を高吸水性樹脂と炭酸カルシウム、塩化
カルシウムで包括固定化した固定化硝化菌を入れてエア
レージジンを行うことにより、生物酸化池2において未
反応のアンモニア性窒素及び不完全硝化により生成する
亜硝酸性窒素が硝酸性窒素に変化する。アンモニア性窒
素は塩素と反応して著しく塩素を消費させるが、硝酸性
窒素は塩素と反応しないので、通常の浄化プロセスにお
ける前塩素処理装置(第1図)が不必要となる。The immobilized nitrification tank 3 contains immobilized nitrifying bacteria that have been selectively cultured in an ammonia-based medium and is comprehensively immobilized with a super absorbent resin, calcium carbonate, and calcium chloride, and performs airage gin to achieve biological oxidation. In pond 2, unreacted ammonia nitrogen and nitrite nitrogen generated by incomplete nitrification change to nitrate nitrogen. Ammonia nitrogen reacts with chlorine, resulting in significant chlorine consumption, but nitrate nitrogen does not react with chlorine, thereby eliminating the need for a pre-chlorination device (FIG. 1) in the normal purification process.
硝化槽3で処理された水は、通常の浄水プロセスである
、急速撹拌池4、沈澱池5、ろ通油6において主として
濁質が除去される。From the water treated in the nitrification tank 3, suspended matter is mainly removed in a rapid stirring tank 4, a sedimentation tank 5, and a filtered oil 6, which are normal water purification processes.
次に、ろ通油6よりの水は、逆浸透装置7の逆浸透膜を
透過することにより溶解性有機物及びイオンが除去され
、塩素注入装置8により塩素殺菌されて配水池9に送ら
れて配水される。Next, the water from the filtration oil 6 is passed through the reverse osmosis membrane of the reverse osmosis device 7 to remove soluble organic matter and ions, sterilized with chlorine by the chlorine injection device 8, and sent to the distribution reservoir 9. Water will be distributed.
一方、逆浸透装置7における逆浸透膜非透過の濃縮水は
脱イオン装置IOによりイオンが除去された後、水道原
水に返送されて原水と混合されて再び沈砂池1に入り浄
水処理される。On the other hand, the concentrated water that does not pass through the reverse osmosis membrane in the reverse osmosis device 7 has its ions removed by the deionization device IO, is returned to the tap water, is mixed with the raw water, and then enters the settling tank 1 again for water purification treatment.
脱イオン装置10のイオン交換樹脂が飽和して脱イオン
能力が低下した場合、洗浄を行う。洗浄した液は洗浄槽
11において石灰を加えて重金属イオンを共沈させ中和
させて、その上澄液を固定化脱窒槽12において、濃縮
硝酸イオンを窒素ガスに変えさせて脱窒し河川等に排水
する。固定化脱窒槽12は、脱窒菌培地により選択培養
した脱窒菌を高吸水性樹脂、炭酸カルシウム、塩化カル
シウムを用いて包括固定化脱窒菌を入れメタノールを基
質として供給するようになっている。When the ion exchange resin in the deionization device 10 becomes saturated and the deionization ability decreases, cleaning is performed. The washed liquid is neutralized by adding lime in the washing tank 11 to coprecipitate heavy metal ions, and the supernatant liquid is immobilized in the denitrification tank 12, where the concentrated nitrate ions are converted into nitrogen gas and denitrified, and then used in rivers, etc. Drain to. The immobilization denitrification tank 12 contains entrapping immobilization of denitrification bacteria selectively cultured in a denitrification bacteria medium using a super absorbent resin, calcium carbonate, and calcium chloride, and is supplied with methanol as a substrate.
H2発明の効果
本発明は、上述のとおり構成されているので、次に記載
する効果を奏する。H2 Effects of the Invention Since the present invention is configured as described above, it produces the following effects.
■ 生物酸化及び硝化により水道原水中の有機物及びア
ンモニア性窒素が減少し、浄水処理における塩素注入量
を低減できる。その結果、健康に有害なトリハロメタン
の生成量を低下させることができる。■ Biological oxidation and nitrification reduce organic matter and ammonia nitrogen in raw water, making it possible to reduce the amount of chlorine injection during water purification. As a result, the amount of trihalomethane produced, which is harmful to health, can be reduced.
■ 硝化菌は独立栄養閑であり、増殖速度が遅く、又低
水温では硝化活性が低下するので、通常の活性汚泥法で
は冬期は硝化率が低下することが多いが、固定化により
硝化菌の濃度を高めであるので、冬期でも硝化率が低下
することがなく、アンモニア性濃度を低下させることが
できる。又、これにより塩素注入量の変化が少なく安定
した浄水処理が行える。■ Since nitrifying bacteria are autotrophic, their growth rate is slow, and their nitrification activity decreases at low water temperatures, the nitrification rate often decreases in winter with the normal activated sludge method, but immobilization reduces the nitrification rate. Since the concentration is high, the nitrification rate does not decrease even in winter, and the ammonia concentration can be lowered. Moreover, this allows stable water purification treatment with little change in the amount of chlorine injected.
■ 逆浸透法では大量の非透過濃縮水の処理が問題とな
るが、これを脱イオン化して水道原水に返送することに
より浄水して利用可能となる。■ With reverse osmosis, there is a problem with processing large amounts of unpermeated concentrated water, but by deionizing this and returning it to the raw water supply, the water can be purified and used.
■ 浄水処理水の水質は、溶解性有機物及びイオンが除
去されて従来よりも高度の水質になる。■ The water quality of purified water is higher than that of conventional water as soluble organic matter and ions are removed.
■ 寓栄養化の原因となる硝酸性窒素及び有害な重金属
が除去される。■ Nitrate nitrogen and harmful heavy metals, which cause trophication, are removed.
■ 下水2次処理水の脱窒、脱リン、濁質、可溶性有機
物及び無機イオンの除去などの3次処理プロセスとして
利用することができる。■ Secondary treatment of sewage It can be used as a tertiary treatment process such as denitrification, dephosphorization, removal of suspended solids, soluble organic matter, and inorganic ions.
第1図は本発明浄水装置の浄水工程図、第2図は従来浄
水装置の浄水工程図である。FIG. 1 is a water purification process diagram of the water purification apparatus of the present invention, and FIG. 2 is a water purification process diagram of a conventional water purification apparatus.
Claims (1)
床型生物酸化池と、 この生物酸化池処理水が導入される高吸水性樹脂に硝化
菌を固定化した固定化硝化槽と、 この硝化槽の処理水が導入される急速撹拌池と、この撹
拌池の撹拌された水が導入される沈澱池と、 この沈澱池の水が導入されるろ過池と、 このろ過池の水が導入される逆浸透装置と、この逆浸透
装置の逆浸透膜透過水が導入される配水池と、 前記逆浸透膜透過水に塩素を注入する塩素注入装置と、 前記逆浸透膜非透過濃縮水のイオンを除去し水道原水中
に返送するイオン交換樹脂を用いた脱イオン装置と、 前記イオン交換樹脂を洗浄した液に石灰を加えて撹拌沈
澱させる洗浄液槽と、 この洗浄液槽の上澄水に固定化脱窒菌を入れメタノール
を基質として供給し脱窒して放流する固定化脱窒槽と、 よりなることを特徴とする浄水処理装置。(1) A settling basin into which raw water from the water supply is introduced; a fixed-bed biological oxidation pond with immobilized activated sludge into which water from the settling basin is introduced; and a super absorbent resin into which treated water from the biological oxidation pond is introduced. An immobilized nitrification tank in which nitrifying bacteria are immobilized, a rapid stirring tank into which the treated water from this nitrification tank is introduced, a settling tank into which the agitated water from this stirring tank is introduced, and a settling tank in which the water from this settling tank is A filtration pond to be introduced, a reverse osmosis device to which water from this filtration pond is introduced, a distribution reservoir to which reverse osmosis membrane permeated water of this reverse osmosis device is introduced, and chlorine injected into the reverse osmosis membrane permeated water. a chlorine injection device; a deionization device using an ion exchange resin that removes ions from the concentrated water that has not permeated through the reverse osmosis membrane and returns it to the tap raw water; and a deionization device that uses an ion exchange resin to remove ions from the concentrated water that has not permeated through the reverse osmosis membrane and to add lime to the liquid from which the ion exchange resin has been washed and stir it for sedimentation. A water purification treatment device comprising: a cleaning liquid tank that contains immobilized denitrifying bacteria in supernatant water of the cleaning liquid tank, supplies methanol as a substrate, denitrifies the water, and discharges the water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63320136A JP2580751B2 (en) | 1988-12-19 | 1988-12-19 | Water purification equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63320136A JP2580751B2 (en) | 1988-12-19 | 1988-12-19 | Water purification equipment |
Publications (2)
Publication Number | Publication Date |
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JPH02164500A true JPH02164500A (en) | 1990-06-25 |
JP2580751B2 JP2580751B2 (en) | 1997-02-12 |
Family
ID=18118109
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Application Number | Title | Priority Date | Filing Date |
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JP63320136A Expired - Lifetime JP2580751B2 (en) | 1988-12-19 | 1988-12-19 | Water purification equipment |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05185095A (en) * | 1992-01-10 | 1993-07-27 | Ngk Insulators Ltd | Water purifying treatment using membrane |
JPH05185093A (en) * | 1992-01-10 | 1993-07-27 | Ngk Insulators Ltd | Method for purifying water by using membrane |
EP1323680A1 (en) * | 2001-12-11 | 2003-07-02 | Ionics Italba S.P.A. | Method for recovering nitrates from percolating waters coming from solid urban waste materials |
WO2004011377A2 (en) * | 2002-07-26 | 2004-02-05 | The Regents Of The University Of California | Treatment of wastewater by biological and membrane separation technologies |
JP2006095363A (en) * | 2004-09-28 | 2006-04-13 | Kurita Water Ind Ltd | Treatment apparatus of wastewater containing organic nitrogen compound |
JP2006181445A (en) * | 2004-12-27 | 2006-07-13 | Kurita Water Ind Ltd | Waste water treatment apparatus |
KR101299352B1 (en) * | 2004-12-14 | 2013-08-22 | 쿠리타 고교 가부시키가이샤 | Apparatus for treating waste water |
CN106336029A (en) * | 2016-09-30 | 2017-01-18 | 东莞市亿霖环保科技有限公司 | Mobile sewage treatment device and control method |
-
1988
- 1988-12-19 JP JP63320136A patent/JP2580751B2/en not_active Expired - Lifetime
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05185095A (en) * | 1992-01-10 | 1993-07-27 | Ngk Insulators Ltd | Water purifying treatment using membrane |
JPH05185093A (en) * | 1992-01-10 | 1993-07-27 | Ngk Insulators Ltd | Method for purifying water by using membrane |
EP1323680A1 (en) * | 2001-12-11 | 2003-07-02 | Ionics Italba S.P.A. | Method for recovering nitrates from percolating waters coming from solid urban waste materials |
WO2004011377A2 (en) * | 2002-07-26 | 2004-02-05 | The Regents Of The University Of California | Treatment of wastewater by biological and membrane separation technologies |
WO2004011377A3 (en) * | 2002-07-26 | 2004-07-22 | Univ California | Treatment of wastewater by biological and membrane separation technologies |
US7045063B2 (en) | 2002-07-26 | 2006-05-16 | The Regents Of The University Of California | Treatment of swine wastewater by biological and membrane separation technologies |
JP2006095363A (en) * | 2004-09-28 | 2006-04-13 | Kurita Water Ind Ltd | Treatment apparatus of wastewater containing organic nitrogen compound |
JP4655570B2 (en) * | 2004-09-28 | 2011-03-23 | 栗田工業株式会社 | Wastewater treatment equipment containing organic nitrogen compounds |
KR101299352B1 (en) * | 2004-12-14 | 2013-08-22 | 쿠리타 고교 가부시키가이샤 | Apparatus for treating waste water |
KR101352247B1 (en) * | 2004-12-14 | 2014-01-15 | 쿠리타 고교 가부시키가이샤 | Apparatus for treating waste water |
JP2006181445A (en) * | 2004-12-27 | 2006-07-13 | Kurita Water Ind Ltd | Waste water treatment apparatus |
CN106336029A (en) * | 2016-09-30 | 2017-01-18 | 东莞市亿霖环保科技有限公司 | Mobile sewage treatment device and control method |
Also Published As
Publication number | Publication date |
---|---|
JP2580751B2 (en) | 1997-02-12 |
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