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JP4190986B2 - Method and apparatus for producing drinking water - Google Patents
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JP4190986B2 - Method and apparatus for producing drinking water - Google Patents

Method and apparatus for producing drinking water Download PDF

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JP4190986B2
JP4190986B2 JP2003315645A JP2003315645A JP4190986B2 JP 4190986 B2 JP4190986 B2 JP 4190986B2 JP 2003315645 A JP2003315645 A JP 2003315645A JP 2003315645 A JP2003315645 A JP 2003315645A JP 4190986 B2 JP4190986 B2 JP 4190986B2
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重信 井川
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Description

この発明は、原水中のミネラル成分を残存させて浄化されており、生活用水や食品工業用水などにも使用可能な飲料水の製造方法およびその製造装置に関する。   The present invention relates to a method and apparatus for producing drinking water that has been purified by leaving mineral components in raw water, and that can be used for domestic water, food industry water, and the like.

一般に、飲料水に無機鉱物質を接触させてミネラル含有量を調整し、または不足する成分を補って健康に良いものとし、また味覚的にも優れた飲料水を製造できることが知られている。   In general, it is known that an inorganic mineral substance can be brought into contact with drinking water to adjust the mineral content, or to supplement a deficient component so as to be healthy, and to produce a drinking water excellent in taste.

従来の飲料水製造装置は、浄水器と同様な構造の透水性カートリッジに、珊瑚砂(コーラルサンド)や石灰岩などの天然ミネラル材を充填して、濾過とミネラル材の溶出を同時に行ない、さらにミネラル成分の溶出量を電気伝導度で検出して調節したミネラル成分量の溶出安定化を図ったものが知られている(特許文献1参照。)。   Conventional drinking water production equipment is filled with water-permeable cartridges with the same structure as a water purifier and filled with natural mineral materials such as coral sand and limestone, and simultaneously filters and elutes mineral materials. The thing which aimed at the elution stabilization of the mineral component amount which detected and adjusted the elution amount of the component with electrical conductivity is known (refer patent document 1).

また、水分子のクラスターのダウンサイジング化を図って水を活性化させる部材として、Na,Al,Si,S,K,Ca,TiおよびFeを主成分として酸化物換算で95重量%以上含有する鉱物微粉100重量部に対して、リン化チタン1〜4重量部、酸化マンガン3〜5重量部および磁鉄鉱1〜2重量部を必須成分として含有する釉薬で、担体粒子表面を被覆して焼成されたセラミックス製の水活性化部材が知られている(特許文献2参照。)。   Further, as a member for activating water by downsizing the water molecule cluster, Na, Al, Si, S, K, Ca, Ti, and Fe are contained as main components in an amount of 95% by weight or more in terms of oxides. A powder containing 1 to 4 parts by weight of titanium phosphide, 3 to 5 parts by weight of manganese oxide, and 1 to 2 parts by weight of magnetite as essential components for 100 parts by weight of fine mineral powder. A ceramic water activation member is known (see Patent Document 2).

また、水道水のその他の飲用水の防臭、除塵および除菌処理に用いられるフィルタとしては、多孔質中空糸膜が良く知られている(特許文献1参照)。   Moreover, a porous hollow fiber membrane is well known as a filter used for deodorization, dust removal and sterilization treatment of tap water and other drinking water (see Patent Document 1).

特開平7−256275号公報(請求項1、段落0003、0004)JP 7-256275 A (Claim 1, paragraphs 0003 and 0004)

特許第2999769号公報(請求項1)Japanese Patent No. 2999769 (Claim 1)

しかし、上記した従来のミネラル剤を用いた飲料水の製造方法では、多孔質化された表面に水の接触通過する際の抵抗が大きく、そのために相当に加圧された水を用いるか、または濾過材から水が徐々に染み出るように大型化したものを設置しなければならず、短時間でミネラル成分を充分に溶出できるものではなかった。   However, in the method for producing drinking water using the above-described conventional mineral agent, the resistance when passing through the water on the porous surface is large, and therefore water that is considerably pressurized is used, or It was necessary to install a large one so that water gradually oozes out from the filter medium, and the mineral component could not be sufficiently eluted in a short time.

また、中空糸膜からなる除菌フィルタは、樹脂製フィルタであるから、塩類やイオンが吸着分離されやすく、飲用水の旨みが感じられるミネラル成分まで除去されてしまう場合があり、確実に除菌されかつ美味しく感じられるミネラル成分を残存させて浄化された鉱水(ミネラルウォータ)を製造できなかった。   In addition, since the sterilization filter made of a hollow fiber membrane is a resin filter, salts and ions are easily adsorbed and separated, and even mineral components that feel the taste of potable water may be removed. However, it was not possible to produce mineral water (mineral water) that was purified by leaving the mineral components that were tasted and felt delicious.

そこで、この発明の課題は、上記した問題点を解決して、ミネラル含有原水中の適当なミネラル成分を残して、短時間に効率よく浄化できる飲料水の製造方法およびその製造装置とすることである。   Then, the subject of this invention solves the above-mentioned problem, and makes it the manufacturing method and the manufacturing apparatus of the drinking water which can purify efficiently in a short time leaving the suitable mineral component in mineral containing raw water. is there.

上記の課題を解決するために、この発明では、SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共にCaとNaとMgとKを合計量で5〜15重量%含有するセラミックス組成物で形成されたセラミックス材に、原水を接触通過させる工程と、この工程を経て生成した鉱水から懸濁物および溶存ガスを無機質系フィルタで分離除去する工程を設け、次いで多孔質セラミックスからなるフィルタでろ過する除菌工程を設けてなる飲料水の製造方法としたのである。 In order to solve the above problems, the present invention contains SiO 2 : 55 to 75% by weight, Al 2 O 3 : 7.5 to 20% by weight and Fe: 3 to 10% by weight, and Ca and Na. A step of bringing raw water into contact with a ceramic material formed with a ceramic composition containing 5 to 15% by weight of Mg and K in a total amount, and a suspension and dissolved gas from mineral water produced through this step A process for separating and removing with a filter is provided, and then a sterilization process for filtering with a filter made of porous ceramics is provided.

上記したように構成されるこの発明の製造方法によると、所定のミネラル成分を含んだ原水はセラミックス材と効率よく接触するなどして活性化され、その後、微小懸濁物や遊離塩素などの溶存ガスが、活性炭やゼオライトからなる無機質系フィルタで分離除去され、さらにトリハロメタン、亜硝酸イオン、ダイオキシン、農薬、菌類などの有機物は多孔質セラミックスからなるフィルタでろ過されて分離除去されるが、前記溶出するか、または原水中に存在していたナトリウム、カルシウム、マグネシウム、カリウムは適量残存した状態で良質の飲料水が得られる。   According to the manufacturing method of the present invention configured as described above, raw water containing a predetermined mineral component is activated by, for example, efficiently contacting with a ceramic material, and then dissolved in a micro suspension or free chlorine. Gas is separated and removed by an inorganic filter made of activated carbon or zeolite, and organic substances such as trihalomethane, nitrite ions, dioxins, agricultural chemicals, and fungi are filtered and removed by a filter made of porous ceramics. Or, good quality drinking water can be obtained with the proper amount of sodium, calcium, magnesium and potassium remaining in the raw water remaining.

また、上記した製造方法に用いる装置としては、SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共にCaとNaとMgとKを合計量で5〜15重量%含有するセラミックス材を通水管内に収容し、この通水管の一端は原水の供給路に接続すると共に、他端には原水が前記セラミックス材に接触通過して生じた鉱水を濾過する無機質材からなるガス吸着性フィルタを接続し、次いで多孔質セラミックス製の除菌用フィルタを接続して設けてなる飲料水の製造装置を使用することが適当である。 As the apparatus used in the manufacturing method described above, SiO 2: 55 to 75 wt%, Al 2 O 3: 7.5~20 wt% and Fe: Ca, Na and Mg with containing 3 to 10 wt% A ceramic material containing 5 to 15% by weight of K and K is accommodated in a water pipe, and one end of this water pipe is connected to the raw water supply path, and the raw water is in contact with the ceramic material at the other end. It is appropriate to use a drinking water production apparatus in which a gas adsorbing filter made of an inorganic material for filtering the generated mineral water is connected and then a porous ceramic disinfecting filter is connected. .

一端が原水の供給路に接続された通水管に所定のセラミックス組成物からなるセラミックス材を収容しておくと、これを通過した後の水には、前記特許文献1に記載された発明と同様の作用により何らかの物理化学的作用によって、界面活性作用の増加、水酸化イオンの増加、水のクラスターのダウンサイジング、すなわち単分子化などの活性化が起こっていると考えられる。   When a ceramic material made of a predetermined ceramic composition is housed in a water pipe having one end connected to the supply path of raw water, the water after passing through this is the same as the invention described in Patent Document 1 above. It is considered that activation of surface activity, increase of hydroxide ions, downsizing of water cluster, that is, monomolecularization, etc. is caused by some physicochemical action due to the action of.

通水管の出口側の端部には無機質材からなるガス吸着性フィルタが接続され、これにより塵埃および遊離塩素などの溶存ガスが除去され、さらに接続された多孔質セラミックス製の除菌用フィルタでトリハロメタン、亜硝酸イオン、ダイオキシン、農薬、菌類などが除去されるが、ここでも前記ミネラル成分は残存する。   A gas-adsorbing filter made of an inorganic material is connected to the end of the water pipe at the outlet side, so that dissolved gases such as dust and free chlorine are removed. Trihalomethane, nitrite ions, dioxins, pesticides, fungi, and the like are removed, but the mineral components still remain here.

原水の連続供給状態でこのような効果を確実にするためには、通水管の管長が、内径の50〜300倍に形成されている上記の飲料水の製造装置とすることが好ましい。   In order to ensure such an effect in the state of continuous supply of raw water, it is preferable to use the above-described drinking water production apparatus in which the length of the water pipe is 50 to 300 times the inner diameter.

また、飲料水の製造装置を小型化するために、通水管の内部に通水管と同長の仕切り壁を挿入して3通路以上に分割して設けると共に、全通路を経由して水が通過するように通水管の両端部にて通路同士を連結したミネラルウォータの製造装置とすることが好ましい。   In addition, in order to reduce the size of the drinking water production apparatus, a partition wall having the same length as the water pipe is inserted into the water pipe and divided into three or more passages, and water passes through all the passages. Thus, it is preferable to provide a mineral water manufacturing apparatus in which the passages are connected to each other at both ends of the water pipe.

さらに好ましくは通水管内の軸方向に小径管を設け、この小径管の周囲に通水管内周面と密接する螺旋状の鍔(またはフィン)を形成すると共に、前記通水管と小径管の間に形成された螺旋状の通水路にリン化チタン、酸化マンガンおよび磁鉄鉱を必須成分として含有する釉薬で被覆して焼成されたセラミックス粒を充填し、前記螺旋状通水路の一端には原水の供給路を接続すると共に、その他端と小径管とを接続して小径管から鉱水を採水する請求項2または3に記載のミネラルウォータの製造装置とすれば、より小型の通水管を採用することができる。   More preferably, a small-diameter pipe is provided in the axial direction in the water pipe, and a spiral ridge (or fin) is formed around the small-diameter pipe so as to be in close contact with the inner peripheral surface of the water pipe, and between the water pipe and the small-diameter pipe. The spiral water passage formed in the container is filled with ceramic grains coated and fired with a glaze containing titanium phosphide, manganese oxide and magnetite as essential components, and one end of the spiral water passage is supplied with raw water The mineral water production apparatus according to claim 2 or 3, wherein the mineral water is collected from the small diameter pipe by connecting the other end and the small diameter pipe, and adopting a smaller water pipe. Can do.

また、前記した除菌作用が優れた多孔質セラミックス製除菌フィルタとしては、SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共にCaとNaとMgとKを合計量で5〜15重量%含有するセラミックス組成物で形成され、表面にSiO2またはAl23の表面層を有する多孔質セラミックス製除菌フィルタを採用した飲料水の製造装置が好ましいものである。 Moreover, as a sterilization filter made of porous ceramics having an excellent sterilization effect as described above, SiO 2 : 55 to 75% by weight, Al 2 O 3 : 7.5 to 20% by weight and Fe: 3 to 10% by weight A porous ceramic disinfecting filter formed of a ceramic composition containing 5 to 15% by weight of Ca, Na, Mg and K in a total amount and having a surface layer of SiO 2 or Al 2 O 3 on the surface. The adopted drinking water production apparatus is preferred.

この発明は、以上説明したように、所定のセラミックス組成物で形成されたセラミックス材に、原水を接触通過させ、生成した活性水から懸濁物および溶存ガスを無機質系フィルタで分離除去し、次いで多孔質セラミックスからなるフィルタでろ過する除菌工程を設けたので、セラミックス材に接触通過するときの水の抵抗が小さくなり、しかも適当なミネラル成分を残し、かつ夾雑物を除去して浄化された飲料水の製造方法になるという利点がある。   In the present invention, as described above, raw water is brought into contact with a ceramic material formed of a predetermined ceramic composition, and suspended and dissolved gases are separated and removed from the generated active water using an inorganic filter, Since a sterilization process for filtering with a filter made of porous ceramics is provided, the resistance of water when passing through the ceramic material is reduced, and the appropriate mineral components are left and impurities are removed for purification. There is an advantage that it becomes a manufacturing method of drinking water.

また、所定のセラミックス組成物で形成されたセラミックス材を通水管内に収容し、この通水管に除塵用フィルタおよび無機質材からなるガス吸着性フィルタを接続し、次いで多孔質セラミックス製の除菌用フィルタに接続した飲料水の製造装置としたので、原水中の適当なミネラル成分が残存しており、しかもトリハロメタン、亜硝酸イオン、ダイオキシン、農薬、菌類などの有機物が分離除去された安全性の高い飲料水を製造できる装置であるという利点がある。   In addition, a ceramic material formed of a predetermined ceramic composition is accommodated in a water pipe, and a dust removing filter and a gas adsorbing filter made of an inorganic material are connected to the water pipe, and then a porous ceramic-made disinfectant is used. Because it is a drinking water production device connected to a filter, suitable mineral components remain in the raw water, and organic substances such as trihalomethane, nitrite ions, dioxins, agricultural chemicals, and fungi are separated and removed. There is an advantage that it is an apparatus which can manufacture drinking water.

飲料水の製造装置において、通水管が所定の内径で所定の管長のものは、上記利点に加えて効率よく飲料水を連続的に製造できるものになる。   In the drinking water manufacturing apparatus, a water pipe having a predetermined inner diameter and a predetermined pipe length can efficiently produce drinking water in addition to the above advantages.

また、通水管の内部を分割して複数の通路を設けたものや、通水管内に螺旋状通水路を設けた飲料水の製造装置では、上記の利点に加えて通水管などを極めて小型化することができるので、製造装置全体を充分に小型化できる利点がある。   In addition, in addition to the above-mentioned advantages, water pipes and other equipment are extremely miniaturized in parts that divide the interior of the water pipe and provide a plurality of passages, and in drinking water production devices that have a spiral water passage in the water pipe. Therefore, there is an advantage that the entire manufacturing apparatus can be sufficiently downsized.

また、多孔質セラミックス製除菌フィルタが、所定のセラミックス組成物で形成されているものは、除菌能力が安定して高いため、極めて安全な飲料水を製造できるものになる。   In addition, when the porous ceramic sterilization filter is formed of a predetermined ceramic composition, the sterilization ability is stable and high, and therefore extremely safe drinking water can be produced.

この発明の実施形態の飲料水の製造装置および製造方法を以下に、添付図面に基づいて説明する。
図1〜4に示すように、第1実施形態の飲料水の製造装置は、セラミックス材1を通水管2の内部に収容し、通水管2の一端は原水である水道水の供給路(矢印)3に接続すると共に、他端には原水が前記セラミックス材に接触通過して活性化された水を、濾過する無機質材からなるガス吸着性フィルタ4を接続し、次いで多孔質セラミックス製の除菌用フィルタ5を接続しており、要所には除塵用フィルタ6を配置したものである。なお、図1中の符号7は、適宜に開閉可能な調整バルブを示している。
A drinking water production apparatus and production method according to embodiments of the present invention will be described below with reference to the accompanying drawings.
As shown in FIGS. 1-4, the manufacturing apparatus of the drinking water of 1st Embodiment accommodates the ceramic material 1 in the inside of the water pipe 2, and the one end of the water pipe 2 is the supply path of the tap water which is raw water (arrow) ) 3 and a gas adsorbing filter 4 made of an inorganic material for filtering the water activated by passing through the ceramic material in contact with the other end of the ceramic material. The filter 5 for bacteria is connected and the filter 6 for dust removal is arrange | positioned in the important point. In addition, the code | symbol 7 in FIG. 1 has shown the adjustment valve which can be opened and closed suitably.

セラミックス材は、SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共にCaとNaとMgとKを合計量で5〜15重量%含有するセラミックス組成物で形成されたものである。セラミックス材は均質に一体成形しても良いが、少なくとも表面がこのようなセラミックスで形成されていればよいので、高温に耐える種々の基材の表面に釉薬(上薬)を塗布し、これを焼成することによって少なくとも表面を所定のセラミックスで形成することができる。 The ceramic material contains SiO 2 : 55 to 75% by weight, Al 2 O 3 : 7.5 to 20% by weight and Fe: 3 to 10% by weight, and 5 to 5 in total of Ca, Na, Mg and K. It is formed of a ceramic composition containing 15% by weight. The ceramic material may be integrally formed integrally, but at least the surface only needs to be formed of such ceramics, so that glaze (supplement) is applied to the surface of various substrates that can withstand high temperatures. By firing, at least the surface can be formed of a predetermined ceramic.

このようなセラミックス組成物の例として、具体的には花崗岩を主成分とするものを採用できる。花崗岩の組成は、例えばNa2O:1.0〜2.5重量%、MgO:1.0〜2.5重量%、Al23:13〜20重量%、SiO2:55〜70重量%、SO3:1.0〜2.0重量%、K2O:3〜4重量%、CaO:2〜4重量%、TiO2:0.5〜1.2重量%およびFe23:7〜15重量%である。 As an example of such a ceramic composition, specifically, a composition mainly composed of granite can be adopted. The composition of granite is, for example, Na 2 O: 1.0 to 2.5 wt%, MgO: 1.0 to 2.5 wt%, Al 2 O 3 : 13 to 20 wt%, SiO 2 : 55 to 70 wt%. %, SO 3: 1.0 to 2.0 wt%, K 2 O: 3~4 wt%, CaO: 2 to 4 wt%, TiO 2: 0.5 to 1.2 wt% and Fe 2 O 3 : 7 to 15% by weight.

図2に示すように、粒状セラミックス材1aに形成するには、例えば直径3〜12mm程度の球状粒に形成したものを採用できる。また、無機質の発泡体や焼結体を基材として用いる場合は、通気孔20μm〜1mm程度の連通気孔を有する多孔質材であることが好ましい。   As shown in FIG. 2, in order to form in the granular ceramic material 1a, what was formed in the spherical particle about 3-12 mm in diameter, for example can be employ | adopted. Moreover, when using an inorganic foam and a sintered compact as a base material, it is preferable that it is a porous material which has a continuous air hole of about 20 micrometers-1 mm of air holes.

また図3に示すように、ミネラル抽出用セラミックス材を管の内部に設けた格子の表面に釉薬として被覆し、焼成することによって、格子状セラミックス材1bその他のハニカム状セラミックス材などに形成することもできる。格子の間隔や孔径は、例えば0.5〜2mmにすると水との接触効率がよくて好ましい。   Also, as shown in FIG. 3, a ceramic material for mineral extraction is coated as a glaze on the surface of a lattice provided inside the tube and fired to form a lattice-like ceramic material 1b or other honeycomb-like ceramic material. You can also. For example, the lattice spacing and the hole diameter are preferably 0.5 to 2 mm because of good contact efficiency with water.

また、釉薬として、Na、Mg、Al、Si、S、K、Ca、TiおよびFeを主成分として酸化物換算で95重量%以上含有する鉱物微粉100重量部、リン化チタン(TiP)1〜4重量部、酸化マンガン3〜5重量部および磁鉄鉱1〜2重量部を含んでいるセラミックス組成物を採用することができる。   Further, as glaze, 100 parts by weight of fine mineral powder containing Na, Mg, Al, Si, S, K, Ca, Ti and Fe as main components and containing 95% by weight or more in terms of oxide, titanium phosphide (TiP) 1 to A ceramic composition containing 4 parts by weight, 3-5 parts by weight of manganese oxide and 1-2 parts by weight of magnetite can be employed.

図1に示すように、セラミックス材を収容した通水管2は、直管の端部に多孔板などの透水性の仕切り部品(図示せず。)を設けてセラミックス材を保持しており、このような通水管2を複数本並べて管端部同士をU字状の管継手8などで接続すれば、比較的小さな装置であっても所要の長さに形成され、所要時間かけて濾過できるものになる。   As shown in FIG. 1, the water pipe 2 containing the ceramic material is provided with a water-permeable partition component (not shown) such as a perforated plate at the end of the straight pipe to hold the ceramic material. If a plurality of such water pipes 2 are arranged and the pipe ends are connected by a U-shaped pipe joint 8 or the like, even a relatively small device can be formed to a required length and filtered over a required time. become.

例えば、通水管2は、水の通過速度を10cm/秒以上、接触時間を10秒以上、圧力0.2MPa以上に調整すれば、少量のセラミックスで効率よく活性化された鉱水を製造することができる。また、通水管全体の管長は、管の内径の50〜300倍に形成することが好ましい。管長を内径の50倍未満に形成すると、前記した圧力で水が接触する時間を10秒以上保つことは困難であり、300倍を越えて管長を延長すると、通水抵抗が増加して製造速度が低下して実用性が損なわれる。   For example, the water pipe 2 can produce mineral water efficiently activated with a small amount of ceramics by adjusting the water passage speed to 10 cm / second or more, the contact time to 10 seconds or more, and the pressure to 0.2 MPa or more. it can. Moreover, it is preferable to form the pipe length of the whole water flow pipe 50 to 300 times the inner diameter of the pipe. If the tube length is less than 50 times the inner diameter, it is difficult to keep the water contact time at the above-mentioned pressure for 10 seconds or more. If the tube length is extended beyond 300 times, the water flow resistance increases and the production speed increases. Decreases, impairing practicality.

除塵用フィルタ6は、複数の通水管2が連結された原水のセラミックス材との接触通過工程の中間部分または下流側に設けることが好ましい。このような除塵用フィルタ6は、例えばメッシュ20〜50μm程度の金網や繊維製網状フィルタなどを採用でき、その他の鉱物微粒子やセラミックス微粉末などを除去できれば、その他周知の濾過装置を採用できる。   The dust removal filter 6 is preferably provided at an intermediate portion or a downstream side of the contact passage process with the raw water ceramic material to which a plurality of water pipes 2 are connected. Such a dust removal filter 6 can employ, for example, a wire mesh or a fiber mesh filter having a mesh of about 20 to 50 μm, and other known filtration devices can be employed as long as other mineral fine particles and ceramic fine powder can be removed.

また、ガス吸着性フィルタ4の具体例としては、5μm以下の微粒子を吸着除去できるような活性炭やゼオライトなどの微細な気孔を有する無機多孔質材をフィルタ材として採用できる。   As a specific example of the gas adsorbing filter 4, an inorganic porous material having fine pores such as activated carbon or zeolite that can adsorb and remove fine particles of 5 μm or less can be used as the filter material.

除菌用フィルタ5は、セラミックスの多孔体からなる基材の表面または中間層に、フィルタの濾過性能を決定する気孔径の分離層を形成したものであり、SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共に、CaとNaとMgとKを合計量で5〜15重量%含有するセラミックス組成物で基材を形成し、表面層をSiO2またはAl23で形成し、粒径0.1μm未満の高分子、微生物、金属微粒子をも分離できるものを採用することが好ましい。 The sterilizing filter 5 is formed by forming a separation layer having a pore diameter that determines the filtration performance of the filter on the surface or intermediate layer of a base material made of a ceramic porous body, SiO 2 : 55 to 75% by weight, The base material is made of a ceramic composition containing Al 2 O 3 : 7.5 to 20% by weight and Fe: 3 to 10% by weight and containing 5 to 15% by weight of Ca, Na, Mg and K in total. Preferably, the surface layer is formed of SiO 2 or Al 2 O 3 and a polymer, microorganisms, and metal fine particles having a particle size of less than 0.1 μm can be separated.

多孔質セラミックスは、無機酸化物と300℃以下で焼失する樹脂粉末を混合し、例えば700℃程度で焼成して樹脂を蒸発して取り除き、その後に形成される孔径0.1μm以下の気孔でもって多孔質化したものを採用することができる。   Porous ceramics are a mixture of inorganic oxide and resin powder that burns down at 300 ° C. or lower, and is baked at about 700 ° C. to evaporate and remove the resin. A porous material can be used.

また、多孔質セラミックス製の除菌フィルタが、粒径0.1μm以下のAl23製微粉末を付着させて焼成されたろ過面を有する多孔質セラミックス製除菌フィルタを採用することがより好ましい。 In addition, it is more preferable that the porous ceramic sterilization filter employs a porous ceramic sterilization filter having a filtration surface fired with Al 2 O 3 fine powder having a particle size of 0.1 μm or less. preferable.

このような多孔質セラミックス製除菌用フィルタの基材内部は、前工程で塩素が除去された微生物が繁殖しやすい水が通過するものであるから、水が滞留しにくい構造であることが好ましく、万一の滞留防止のためには、例えば電磁弁で開閉する放水口を設け、中間部から滞留水が適宜に放出されるよう設けることが好ましい。   The inside of the base material of such a porous ceramic sterilization filter is preferably a structure in which water does not stay easily because water through which microorganisms from which chlorine has been removed in the previous step easily propagates passes. In order to prevent stagnation, it is preferable to provide, for example, a water outlet that is opened and closed by a solenoid valve so that the stagnation water is appropriately discharged from the intermediate portion.

このようなフィルタ類を接続して構成された図1に示すようなミネラルを含有する飲料水の製造装置は、飲料水の自動販売機に組み入れて使用することができる。   The apparatus for producing drinking water containing minerals as shown in FIG. 1 configured by connecting such filters can be used by being incorporated into a drinking water vending machine.

すなわち、図1及び図4に示すように、上水道から供給された原水は、U字状の管継手8で接続された直列3連の通水管2の2つ目の通水管2を通過した後、バイパスによりその一部をペットボトルなどの容器9の洗浄水として使用し、洗浄された容器10に対して、製造された飲料水を注入することが好ましい。   That is, as shown in FIG.1 and FIG.4, after the raw | natural water supplied from the waterworks passed through the 2nd water flow pipe 2 of the series 3 water flow pipe 2 connected by the U-shaped pipe joint 8. It is preferable that a part of the water is used as washing water for the container 9 such as a plastic bottle by bypass, and the produced drinking water is injected into the washed container 10.

図4に示した自動販売機では、まず、右側の洗浄口11に容器9を置いて、コインなどを投入してタイマーを働かし、規定時間だけ水で洗い、次いで左側の水受け口12に容器9をおいて、ミネラルを含有する飲料水の必要量だけを持参の容器10に注入して購入することができる。   In the vending machine shown in FIG. 4, first, the container 9 is placed in the right washing port 11, a coin is inserted and the timer is operated, and the container 9 is placed in the left water receiving port 12 by washing with water for a specified time. However, only the required amount of drinking water containing minerals can be injected into the container 10 to be brought in and purchased.

第2実施形態の製造装置としては、図5〜7に示した通水管13を用いたこと以外は、第1実施形態の装置と同じ構成を採用できる。   As a manufacturing apparatus of 2nd Embodiment, the structure same as the apparatus of 1st Embodiment can be employ | adopted except having used the water pipe 13 shown to FIGS.

第2実施形態に用いる通水管13は、その内部に管と略同長の4枚の仕切り壁14、15、15、16を格子状に組み立てて挿入して9つの通路を形成したものであり、管の内周に沿って隣合う2つの通路毎に端部を連絡させ、このようにして全通路を直列に連通させ、すなわち全通路を一巡してから水が管中央の通路から通過させるものである。   The water flow pipe 13 used in the second embodiment has nine partition walls 14, 15, 15, 16 that are approximately the same length as the pipe and are assembled and inserted into a lattice to form nine passages. , The ends of the two adjacent passages along the inner circumference of the pipe are connected to each other, and in this way, all the passages are connected in series, that is, the whole passage is made a round and then water passes from the passage in the center of the pipe. Is.

すなわち、図6、7に示すように、仕切り壁14、15、15、16は、略長方形状の合成樹脂板もしくはセラミックス板または金属板などで形成した板状部品からなり、長手方向の上端もしくは下端または両端の隅部を方形状に切り欠いて水の抜け口17、18、19、20を形成すると共に、組み合わせた板状部品の交差部に細溝状のスリット21を形成しており、図6に示す格子状に組み立てた後、全体を通水管2に挿入してセットする。
なお、仕切り壁の枚数は、適宜に変更することができ、必要に応じて複数の通路を利用できるように構成できる。通水させる順番も前記した水の抜け口の位置により、適宜に変更できる。
That is, as shown in FIGS. 6 and 7, the partition walls 14, 15, 15, and 16 are made of a plate-like component formed of a substantially rectangular synthetic resin plate, a ceramic plate, a metal plate, or the like. The lower end or the corners at both ends are cut into a square shape to form water outlets 17, 18, 19, and 20, and a narrow groove-shaped slit 21 is formed at the intersection of the combined plate-like parts, After assembling into the lattice shape shown in FIG. 6, the whole is inserted into the water pipe 2 and set.
Note that the number of partition walls can be changed as appropriate, and a plurality of passages can be used as necessary. The order of passing water can be changed as appropriate depending on the position of the water outlet.

図8(a)に示すように、管の両端が蓋状部品13aで閉じられた通水管13は、その内部に挿入された仕切り壁14、15、15、16(図5参照)により、矢印aから導入された水を矢印b、c、d、e、f、g、h、iの順に反転させて全通路を一巡して通過させ、矢印jの通路から放出する。   As shown in FIG. 8 (a), the water flow pipe 13 having both ends of the pipe closed by the lid-like part 13a is shown by arrows by partition walls 14, 15, 15, 16 (see FIG. 5) inserted therein. The water introduced from a is reversed in the order of arrows b, c, d, e, f, g, h, i, passes through all the passages, and is discharged from the passages of arrow j.

前述のようにこのような通水管13内には、粒状のセラミックス材が充填されているため、所定成分を含んだセラミックスが原水に効率よく接触し、次工程に送られる。   As described above, since the inside of the water pipe 13 is filled with the granular ceramic material, the ceramic containing the predetermined component efficiently contacts the raw water and is sent to the next process.

図8に示すように、第3実施形態のミネラルウォータの製造装置は、原水を粒状セラミックス材1aに接触通過させる通水管13を設け、仕切り壁14、15、15、16(図5参照)を組み付けて挿入すると共に、その内部中央の通路には懸濁物および溶存ガスを分離除去する活性炭などのガス吸着性フィルタ23を充填した無機質系フィルタと、多孔質セラミックスでろ過する除菌用フィルタ24を直結させて小型化したものであり、通水管13内の中央部の通路内には、活性炭などのガス吸着性フィルタ23を充填すると共に、通水管13は継手22を介して同径の管に収容した多孔質セラミックス製除菌フィルタ24に接続して製造装置を小型化したものである。   As shown in FIG. 8, the manufacturing apparatus of the mineral water of 3rd Embodiment provides the water flow pipe 13 which makes raw water contact the granular ceramic material 1a, and provides partition walls 14, 15, 15, and 16 (refer FIG. 5). Assembling and inserting, an inorganic center filter filled with a gas adsorbing filter 23 such as activated carbon that separates and removes suspended solids and dissolved gas in a passage in the center of the inside thereof, and a sterilization filter 24 that filters with porous ceramics. The central passage in the water conduit 13 is filled with a gas adsorbing filter 23 such as activated carbon, and the water conduit 13 is a tube having the same diameter via a joint 22. The manufacturing apparatus is downsized by connecting to a porous ceramic sterilization filter 24 housed in the container.

また、図9に示すように、第4実施形態のミネラル含有飲料水の製造装置は、通水管部25内の仕切りを連続した螺旋状に形成している。すなわち、このものは通水管部25内に螺旋状鍔付きの小径管26を設け、小径管26の内部には、活性炭などのガス吸着性フィルタ23を装填し、螺旋状鍔27は小径管26の周囲で通水管25の内周面と密接する高さに設け、これにより形成された通水管25と小径管26の間の螺旋状通水路に粒状セラミックス材1aを多数充填している。
そして、螺旋状通水路の最上流部には水道水の供給路28を接続すると共に、螺旋状通水路の最下流部と小径管26とを切り欠いて設けた水抜け口29で連続させて、小径管26内のガス吸着性フィルタ23に接触通過した水が多孔質セラミックス製除菌フィルタ24を通過して飲料水30を得るようにしている。
これらミネラル含有飲料水の製造装置によると、原水中に含まれていたミネラル成分が残存し、しかもトリハロメタン、亜硝酸イオン、ダイオキシン、農薬、菌類などの有機物が分離除去された安全性の高い飲料水を製造でき、しかも通水管などが小型化されている装置は、持ち運びも容易であるから、ミネラル含有の飲料水の自動販売機の外にも家庭用や非常時にも使用できるものである。
Moreover, as shown in FIG. 9, the manufacturing apparatus of the mineral containing drinking water of 4th Embodiment forms the partition in the water flow pipe part 25 in the continuous spiral shape. That is, this is provided with a small-diameter pipe 26 with a spiral hook in the water flow pipe portion 25, and a gas-adsorbing filter 23 such as activated carbon is loaded inside the small-diameter pipe 26, and the helical hook 27 is a small-diameter pipe 26. Is provided at a height close to the inner peripheral surface of the water pipe 25, and the spiral water passage formed between the water pipe 25 and the small diameter pipe 26 is filled with a large number of granular ceramic materials 1 a.
Then, a tap water supply path 28 is connected to the most upstream part of the spiral water passage, and the water outlet 29 is formed by cutting out the most downstream part of the spiral water passage and the small-diameter pipe 26. The water that has passed through the gas adsorbing filter 23 in the small-diameter pipe 26 passes through the porous ceramic sterilization filter 24 to obtain the drinking water 30.
According to these mineral-containing drinking water manufacturing equipment, the mineral components contained in the raw water remain, and the highly safe drinking water from which organic substances such as trihalomethane, nitrite ions, dioxins, agricultural chemicals and fungi are separated and removed. In addition, since the apparatus in which the water pipe and the like are miniaturized can be easily carried, it can be used not only for vending machines containing mineral water but also for home use and emergency.

第1実施形態の飲料水の製造装置を示す説明図Explanatory drawing which shows the manufacturing apparatus of the drinking water of 1st Embodiment. 第1実施形態に用いるセラミックス材の斜視図The perspective view of the ceramic material used for 1st Embodiment 第1実施形態に用いるセラミックス材の斜視図The perspective view of the ceramic material used for 1st Embodiment 第1実施形態の飲料水の製造装置を収容した自動販売機の斜視図The perspective view of the vending machine which accommodated the drinking water manufacturing apparatus of 1st Embodiment. 第2実施形態に用いる通水管の形態を示す斜視図The perspective view which shows the form of the water flow pipe used for 2nd Embodiment. 第2実施形態に用いる仕切り壁を示す斜視図The perspective view which shows the partition wall used for 2nd Embodiment 第2実施形態に用いる仕切り壁を分解して示す正面図The front view which decomposes | disassembles and shows the partition wall used for 2nd Embodiment (a)第3実施形態に用いる通水管と除菌用フィルタの連結状態を示す断面図(b)第3実施形態に用いる通水管の断面図(A) Sectional drawing which shows the connection state of the water flow pipe used for 3rd Embodiment, and the filter for disinfection (b) Cross section of the water flow pipe used for 3rd Embodiment 第4実施形態に用いる通水管と除菌用フィルタの連結状態を一部切り欠いて示す断面図Sectional drawing which partially cuts and shows the connection state of the water flow pipe and sanitization filter which are used for 4th Embodiment

符号の説明Explanation of symbols

1 セラミックス材
1a 粒状セラミックス材
1b 格子状セラミックス材
2、13 通水管
3、28 水道水の供給路
4、23 ガス吸着性フィルタ
5、24 除菌用フィルタ
6 除塵用フィルタ
7 調整バルブ
8 管継手
9、10 容器
11 洗浄口
12 水受け口
14、15、16 仕切り壁
17、18、19、20 水抜け口
21 スリット
22 継手
25 通水管部
26 小径管
27 螺旋状鍔
29 水抜け口
30 飲料水
DESCRIPTION OF SYMBOLS 1 Ceramic material 1a Granular ceramic material 1b Grid-shaped ceramic material 2, 13 Water flow pipe 3, 28 Tap water supply path 4, 23 Gas-adsorbing filter 5, 24 Disinfection filter 6, Dust removal filter 7, Adjustment valve 8 Pipe joint 9 DESCRIPTION OF SYMBOLS 10 Container 11 Washing port 12 Water receiving port 14,15,16 Partition wall 17, 18, 19, 20 Water outlet 21 Slit 22 Joint 25 Water pipe part 26 Small diameter pipe 27 Spiral trough 29 Water outlet 30 Drinking water

Claims (4)

SiO2:55〜75重量%、Al23:7.5〜20重量%およびFe:3〜10重量%を含有すると共にCaとNaとMgとKを合計量で5〜15重量%含有するセラミックス組成物からなるセラミックス材を通水管内に収容し、この通水管の一端は原水の供給路に接続すると共に、他端には前記セラミックス材に接触通過した水を濾過する無機質材製のガス吸着性フィルタを接続し、前記セラミックス組成物で形成され、表面または中間層に孔径0.1μm以下の気孔を形成したSiO2またはAl23分離層を有する多孔質セラミックス製の除菌用フィルタを接続して設けてなる飲料水の製造装置。 SiO 2 : 55 to 75 wt%, Al 2 O 3 : 7.5 to 20 wt% and Fe: 3 to 10 wt%, and 5 to 15 wt% of Ca, Na, Mg and K in total A ceramic material made of a ceramic composition is accommodated in a water pipe, and one end of the water pipe is connected to a supply path of raw water, and the other end is made of an inorganic material for filtering water that has passed through the ceramic material. Disinfection made of porous ceramics having a SiO 2 or Al 2 O 3 separation layer connected to a gas adsorbing filter and formed with the ceramic composition and having pores with a pore size of 0.1 μm or less on the surface or intermediate layer A device for producing drinking water, which is provided by connecting an industrial filter. 通水管が、管長を内径の50〜300倍に形成した通水管である請求項1に記載の飲料水の製造装置。   The drinking water producing apparatus according to claim 1, wherein the water pipe is a water pipe formed with a pipe length 50 to 300 times the inner diameter. 通水管の内部に通水管と同長の仕切り壁を挿入して通路を複数に分割して設けると共に、全通路を経由して水が通過するように各通路を直列に連通させてなる請求項1または2に記載の飲料水の製造装置。   Claims: A partition wall having the same length as the water pipe is inserted into the water pipe to divide the passage into a plurality of parts, and the passages are connected in series so that water passes through all the passages. The drinking water production apparatus according to 1 or 2. 通水管内の軸方向に小径管を設け、この小径管の周囲に通水管内周面と密接する高さの螺旋状鍔を形成すると共に、前記通水管と小径管の間に形成された螺旋状通水路に前記ミネラル抽出用セラミックス材からなるセラミックス粒を充填し、前記螺旋状通水路の一端には原水の供給路を接続すると共に、螺旋状通水路の他端と小径管を接続して小径管から鉱水を採水する請求項1または2に記載の飲料水の製造装置。   A small-diameter pipe is provided in the axial direction in the water pipe, and a spiral ridge having a height close to the inner peripheral surface of the water pipe is formed around the small-diameter pipe, and a spiral formed between the water pipe and the small-diameter pipe. A ceramic channel made of the ceramic material for mineral extraction is filled in the water channel, and a raw water supply channel is connected to one end of the spiral water channel, and a small diameter pipe is connected to the other end of the spiral water channel. The apparatus for producing drinking water according to claim 1 or 2, wherein mineral water is collected from the small-diameter pipe.
JP2003315645A 2003-09-08 2003-09-08 Method and apparatus for producing drinking water Expired - Fee Related JP4190986B2 (en)

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JP5384158B2 (en) * 2009-03-24 2014-01-08 一誠 生田 Drinking water production equipment
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