JP2010221206A - Carried type water-purifying kit - Google Patents

Carried type water-purifying kit Download PDF

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JP2010221206A
JP2010221206A JP2009098443A JP2009098443A JP2010221206A JP 2010221206 A JP2010221206 A JP 2010221206A JP 2009098443 A JP2009098443 A JP 2009098443A JP 2009098443 A JP2009098443 A JP 2009098443A JP 2010221206 A JP2010221206 A JP 2010221206A
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filter
water
cylinder
sand
paper
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Tatsuro Yamamoto
達郎 山本
Atsushi Komagata
淳 駒形
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Mitsubishi Chemical Aqua Solutions Co Ltd
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Wellthy Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a carried type water-purifying kit which can be used outdoors in disaster; which is capable of removing fine grains, dissolved organic substances, algae and general bacteria and so on included as suspended matter in the water source to be purified; which hardly causes clogging in an activated carbon cylinder and a membrane filter for a long time; and whose treatment and maintenance are easy. <P>SOLUTION: The carried type water-purifying kit capable of assembling a simple water-purifying device includes a pump to pump up and deliver the water to be treated; a sand filter cylinder having a quartz sand layer as a filtration layer; an activated carbon cylinder filled with activated carbon and/or a membrane filter; and a piping connecting each constituent. The membrane filter has a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane. Each of the constituents is connected by the piping in the order of the pump, the sand filter cylinder and the activated carbon cylinder and/or the membrane filter. After the water to be treated pumped up by the pump is filtrated by the sand filter cylinder, it passes the activated carbon cylinder and/or the membrane filter to obtain treated water. When being accommodated, each constituent can be accommodated in a case for carrying in a separated state. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、キャンプ・行楽時や、軍用、災害時等に、屋外に携行可能な携行型浄水キットに関する。  The present invention relates to a portable water purification kit that can be carried outdoors during camping and vacation, military use, disasters, and the like.

精密ろ過(MF)膜、限外ろ過(UF)膜又は逆浸透(RO)膜等を使用した携帯用浄水装置を用いた水処理方法では、これまで前処理に様々な装置が実用されていたが、前処理の懸濁物質除去能力を高めると前処理装置が早期に目詰まりし、又前処理装置の懸濁物質除去能力を低くするとMF膜、UF膜、又はRO膜が早々に目詰まりを生じ易いという難点があった。  In the water treatment method using a portable water purification device using a microfiltration (MF) membrane, an ultrafiltration (UF) membrane or a reverse osmosis (RO) membrane, various devices have been put to practical use so far. However, if the suspended matter removal capability of the pretreatment is increased, the pretreatment device is clogged early, and if the suspended material removal capability of the pretreatment device is lowered, the MF membrane, UF membrane, or RO membrane is clogged early. There was a difficulty that it was easy to produce.

また、災害時や軍用の場合には、災害場所や山間部等で飲料水を得ようとすると電気がない場合が考えられ、その場合携帯用浄水装置は水の移動(送水)を手動ポンプに頼ることになる。しかし、往復(ピストン)操作の手動ポンプ等の場合は流れが一定でなく脈動し、手動ポンプの吸引時には流れがないか或いは少なく、吐出時には大きな流れがあるので、MF膜、UF膜又はRO膜の水量負荷が大きく相違するため膜の劣化が早まるという難点があった。例えば、特許文献1に記載のような往復操作のポンプでも、携行用浄水装置に利用するには水量負荷の変動が著しく、手動ポンプは電気が不要で、安価で操作が簡単という利点があるが、未だ改良の余地があった。  Also, in the case of disasters or military use, there may be no electricity when trying to obtain drinking water in disaster areas or mountainous areas, etc. In that case, the portable water purifier uses a manual pump to move water (water supply). Rely on. However, in the case of a manual pump for reciprocating (piston) operation, the flow is not constant and pulsates, and there is no or little flow at the time of suction by the manual pump, and there is a large flow at the time of discharge. There was a problem in that the deterioration of the membrane was accelerated because the water amount load of the water was greatly different. For example, even a reciprocating pump as described in Patent Document 1 has the advantage that the fluctuation of the water load is remarkably used in a portable water purifier, and the manual pump does not require electricity, is inexpensive and easy to operate. There was still room for improvement.

特許第3457301号公報  Japanese Patent No. 3457301

本発明の第1の目的は、キャンプ・行楽時や、軍用、災害時等に屋外に携行し使用可能な膜ろ過器を備えた携行型浄水キットであって、浄化する水源の懸濁物質として含まれる微細粒子、溶存性有機物、藻類及び一般細菌等の除去が可能で、長期に亘り、活性炭筒や膜ろ過器の目詰まりが生じ難く、かつ、取扱いやメンテナンスの容易な携行型浄水キットを提供することにある。
また、第2の目的は、主に電気がない状況で使用する手動ポンプの脈動を低減し、後段の膜ろ過器等にかかる水量負荷を略均一に保持し得るように機能する砂ろ過筒を備えた携行型浄水キットを提供することにある。
また、第3の目的は、紙フィルタカートリッジを備え、紙フィルタカートリッジの交換が容易で単純な構造を有するろ過器を備えた携行型浄水キットを提供することにある。
The first object of the present invention is a portable water purification kit equipped with a membrane filter that can be carried outdoors and used for camping, vacation, military use, disasters, etc., as a suspended substance of the water source to be purified. A portable water purification kit that can remove fine particles, dissolved organic matter, algae, and general bacteria contained in the product, prevents clogging of activated carbon cylinders and membrane filters for a long time, and is easy to handle and maintain. It is to provide.
A second purpose is to reduce the pulsation of a manual pump used mainly in the absence of electricity, and to provide a sand filter cylinder that functions so that the water load on the subsequent membrane filter or the like can be maintained substantially uniformly. The purpose is to provide a portable water purification kit.
A third object is to provide a portable water purification kit including a paper filter cartridge and including a filter having a simple structure in which the paper filter cartridge can be easily replaced.

本発明は、膜ろ過器及び/又は活性炭筒の前段に、ろ過層として石英砂層を有する砂ろ過筒を配置し、該砂ろ過筒によるろ過後に膜ろ過器及び/又は活性炭筒で処理することで、膜ろ過器及び/又は活性炭筒の目詰まりを回避し得、更に砂ろ過筒自体の目詰まりも生じ難いことを見出し、本発明を完成するに至ったものである。  This invention arrange | positions the sand filter cylinder which has a quartz sand layer as a filtration layer in the front | former stage of a membrane filter and / or activated carbon cylinder, and processes by a membrane filter and / or activated carbon cylinder after filtration by this sand filter cylinder. It has been found that clogging of the membrane filter and / or the activated carbon cylinder can be avoided, and that the sand filtration cylinder itself is hardly clogged, and the present invention has been completed.

すなわち、本発明の携行型浄水キットは、被処理水を汲み上げて送水するポンプと、ろ過層として石英砂層を有する砂ろ過筒と、活性炭を充填した活性炭筒及び/又は膜ろ過器と、前記各構成要素を繋ぐ配管と、を有し、前記膜ろ過器は、精密ろ過膜、限外ろ過膜又は逆浸透膜を備え、前記ポンプ、前記砂ろ過筒、前記活性炭筒及び/又は膜ろ過器の順に、前記配管により各構成要素を連結し、ポンプで汲み上げられる被処理水を砂ろ過筒でろ過した後、活性炭筒及び/又は膜ろ過器に通水し、処理水を得る簡易浄水装置を組立可能なキットであって、収容時には、各構成要素を分離した状態で携行用ケース内に収容し得ることを特徴としている。  That is, the portable water purification kit of the present invention includes a pump that pumps up and feeds water to be treated, a sand filter cylinder having a quartz sand layer as a filter layer, an activated carbon cylinder and / or a membrane filter filled with activated carbon, And the membrane filter includes a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane, and the pump, the sand filtration tube, the activated carbon tube, and / or the membrane filter. In order, connect each component by the above-mentioned piping, filter the treated water pumped up by the pump through the sand filter cylinder, and then pass it through the activated carbon cylinder and / or membrane filter to assemble a simple water purification device to obtain treated water It is a possible kit, and is characterized in that each component can be stored in a carrying case in a separated state.

なお、携行用ケースは、特に限定されないが、例えば、リュックサック、スーツケース等の鞄類が挙げられる。また、携行用ケースへの収納容易性の観点から、前記各構成要素は全て円筒型であることが好ましい。  The carrying case is not particularly limited, and examples thereof include bags such as a rucksack and a suitcase. In addition, from the viewpoint of easy storage in the carrying case, it is preferable that all the components are cylindrical.

前記石英砂層が、天然の母岩を破砕して得られる破砕石英砂からなり、500〜850μmの粒径のものを重量で全体の50%以上、好ましくは60〜90%含むことが望ましい。
一般的な海砂、川砂、山砂のように、角がなく、表面が平滑なろ材を使用した際には、ろ過層全体の流路間隙がほぼ同一の単純構成となるので、比較的大きな懸濁物はろ過層上部の表層部で捕捉され、微小懸濁物はろ過層を通過してしまう。しかし、天然の母岩(珪石等)を人工的に粉砕篩分けして得られる破砕石英砂は、表面が荒れているため、大小種々の間隙が生じ、複雑な流路が形成されるので、ろ過層全域で種々の大きさの懸濁物を捕捉し得るため、砂ろ過筒及び後段の膜ろ過器等が一層長期に亘り目詰まりを起こし難くなる。また、粒径が上記範囲のものが上記量含まれると、懸濁物を効率よく排除し得ると共に、砂ろ過筒の目詰まりも生じ難い。
砂ろ過筒によるろ過後のろ過水の濁度が1度以下であることが好ましい。活性炭筒及び/又は膜ろ過器に通水する被処理水の濁度を1度以下とし得るので、後段の活性炭筒や膜ろ過器の目詰まりが生じ離く、長期に亘り、利用可能となる。
なお、砂ろ過筒は、ろ過材(石英砂)を処理水(浄水)中で濯ぐことで、容易に再生可能であり、取扱いも容易である。
The quartz sand layer is made of crushed quartz sand obtained by crushing a natural host rock, and it is desirable to contain a particle having a particle diameter of 500 to 850 μm by 50% or more, preferably 60 to 90% by weight.
When using a filter medium with no corners and a smooth surface, such as general sea sand, river sand, and mountain sand, the flow path gap of the entire filtration layer is almost the same, so it is relatively large. The suspension is trapped at the surface layer above the filtration layer, and the microsuspension passes through the filtration layer. However, since the crushed quartz sand obtained by artificially crushing and sieving natural mother rock (silica stone, etc.) has a rough surface, various large and small gaps are created, and complex flow paths are formed. Since suspensions of various sizes can be captured throughout the filtration layer, the sand filter cylinder and the subsequent membrane filter are less likely to be clogged for a longer period of time. In addition, when the amount of the particles having the above-mentioned range is included in the above amount, the suspended matter can be efficiently removed and the sand filter cylinder is hardly clogged.
It is preferable that the turbidity of filtered water after filtration with a sand filter cylinder is 1 degree or less. Since the turbidity of the water to be treated passing through the activated carbon cylinder and / or the membrane filter can be set to 1 degree or less, the activated carbon cylinder and the membrane filter in the subsequent stage are clogged and can be used for a long time. .
The sand filter cylinder can be easily regenerated and easily handled by rinsing the filter medium (quartz sand) in the treated water (purified water).

前記ポンプが往復動式手動ポンプなどの吐出脈動を生じるポンプであり、前記砂ろ過筒が、該砂ろ過筒内のろ過層の上方に前記ポンプにより送水される被処理水の脈動を低減するための空気層を備えていることが好ましい。  The pump is a pump that generates discharge pulsation such as a reciprocating manual pump, and the sand filter cylinder reduces pulsation of water to be treated which is fed by the pump above the filtration layer in the sand filter cylinder. It is preferable that the air layer is provided.

前記砂ろ過筒は、上部に被処理水を導入する導入口を、下部に処理水を取り出す取出し口を備え、前記ろ過層が、該ろ過層の上方に空気層が設けられるように形成されており、該砂ろ過筒の上部にはさらに前記空気層と連通するように、ろ過筒内に空気を取り入れる空気取り入れ口と、ろ過筒内の圧力が一定圧力を超えた時にろ過筒内の空気を外部に放出するリリース弁とが設けられており、前記ろ過層の最上部近傍の所定位置に、ろ過筒内の水位を調整するための水位調整バルブを備えた排出口が設けられており、被処理水のろ過時においても、前記空気層が常時維持されるよう(常時残存するよう)にろ過筒内の水位と空気量を調節することが好ましい。  The sand filter cylinder is provided with an inlet for introducing the water to be treated at the upper part and an outlet for taking out the treated water at the lower part, and the filtration layer is formed so that an air layer is provided above the filtration layer. An air intake port for taking air into the filter cylinder so as to further communicate with the air layer, and air in the filter cylinder when the pressure in the filter cylinder exceeds a certain pressure. A release valve that discharges to the outside, and a discharge port having a water level adjustment valve for adjusting the water level in the filtration cylinder is provided at a predetermined position near the top of the filtration layer. Even during the filtration of treated water, it is preferable to adjust the water level and the amount of air in the filter cylinder so that the air layer is always maintained (so that it always remains).

前記砂ろ過筒は、前記導入口の下方に該導入口より流入する被処理水の勢いを止め、下方の前記ろ過層上に供給される被処理水を分散する散水板を備えることが好ましい。  It is preferable that the sand filter cylinder includes a watering plate that stops the momentum of the water to be treated flowing from the introduction port below the introduction port and disperses the treatment water supplied onto the filtration layer below.

前記携行型浄水キットが、さらに、前記砂ろ過筒の上流に配置される、使い捨て紙フィルタカートリッジを備えたろ過器を有することが好ましい。  It is preferable that the portable water purification kit further includes a filter provided with a disposable paper filter cartridge disposed upstream of the sand filter cylinder.

前記紙フィルタカートリッジを備えたろ過器が、一端に底部を、他端に開口部を有し、前記底部又は底部近傍にろ過水を取り出す取出し口を有する筒型の容器本体と、前記容器本体内に収容され、平面視略矩形状の扁平な袋状に形成され、一隅に小孔部を有する袋状ろ紙、及び一端が外方に突出するように該小孔部より該袋状ろ紙内に挿入され、該小孔部近傍で密着固定された接続管を有する紙フィルタカートリッジと、前記紙フィルタカートリッジを前記容器本体に収容した際に前記容器本体内に流路となる間隙を形成するための多孔質体からなるシート状のスペーサと、有底筒型で、肉厚の底部に貫通孔を有し、該貫通孔の外方側に内螺子部を有する、前記容器本体の開口部を閉塞する蓋体と、前記内螺子部に螺合可能な外螺子部を一端に備える被処理水を導入する導入管と、を備え、前記ろ過器は、前記蓋体の貫通孔内の内螺子部に、前記導入管を螺合し、該貫通孔の他端側に、前記紙フィルタカートリッジの接続管を挿入することで前記導入管と該接続管を液密に接続し、前記紙フィルタカートリッジを、該紙フィルタカートリッジの袋状ろ紙部に重ね合わせた前記スペーサと共に前記接続管を軸として巻き取った状態で、前記容器本体内に収容し、前記蓋体を該容器本体の開口部に嵌合することで組立てられ、前記導入管から前記接続管を介して前記袋状ろ紙内に被処理水を導入し、該袋状ろ紙を透過したろ過水を前記容器本体底部の取出し口より取り出し、被処理水より取り除いた汚濁物を前記袋状ろ紙内に溜めるようにすることが好ましい。  A filter equipped with the paper filter cartridge has a cylindrical container body having a bottom at one end, an opening at the other end, and an outlet for taking out filtrated water at or near the bottom, and the container body And is formed into a flat bag shape having a substantially rectangular shape in plan view, and a bag-shaped filter paper having a small hole portion at one corner, and the small hole portion into the bag-shaped filter paper so that one end protrudes outward. A paper filter cartridge having a connecting tube inserted and fixed in the vicinity of the small hole, and a gap for forming a flow path in the container body when the paper filter cartridge is accommodated in the container body A sheet-like spacer made of a porous material and a bottomed cylindrical type, having a through hole in the thick bottom, and having an internal screw part on the outer side of the through hole, closing the opening of the container body One end of a cover body and an outer screw portion that can be screwed into the inner screw portion An inlet pipe for introducing the water to be treated, wherein the filter is screwed into the inner screw portion in the through hole of the lid body, and the other end side of the through hole The connection pipe of the paper filter cartridge is inserted into a liquid-tight connection between the introduction pipe and the connection pipe, and the connection pipe is connected to the paper filter cartridge together with the spacer superimposed on the bag-shaped filter paper portion of the paper filter cartridge. The bag-like filter paper is accommodated in the container main body in a state of being wound around the shaft, and is assembled by fitting the lid body into the opening of the container main body, through the connecting pipe from the introduction pipe Introducing the water to be treated, taking out the filtered water that has passed through the bag-shaped filter paper from the outlet at the bottom of the container body, and collecting the contaminants removed from the water to be treated in the bag-shaped filter paper. preferable.

前記多孔質体からなるシート状のスペーサとしては、例えば不織布が用いられる。前記スペーサは、前記袋状ろ紙の平面視形状とほぼ同じ大きさか、或いはそれより若干大きいことが好ましい。これによれば、巻き取った袋状ろ紙内に被処理水が導入され、膨らんだ際にも処理水の流路となる不織布が巻き取った袋状ろ紙間に埋まってしまうことがないので、重なり合った袋状ろ紙の外周に確実に処理水を通過させるための処理水流路を形成することが可能となる。  As the sheet-like spacer made of the porous body, for example, a nonwoven fabric is used. The spacer is preferably approximately the same size as or slightly larger than the shape of the bag-shaped filter paper in plan view. According to this, the water to be treated is introduced into the wound bag-shaped filter paper, and when it swells, the nonwoven fabric that becomes the flow path of the treated water is not buried between the wound bag-shaped filter paper, It becomes possible to form a treated water channel for reliably passing treated water around the outer periphery of the overlapping bag-shaped filter paper.

前記袋状ろ紙が、パルプとPETの混繊維からなり、熱ローラによる加熱・加圧処理がされ、該処理後の厚みが50〜70μmであるろ紙を袋状に成形して製造されており、かつ、表面に撥水処理がされていないことが好ましい。  The bag-shaped filter paper is made of a mixed fiber of pulp and PET, heated and pressurized by a heat roller, and manufactured after forming the filter paper having a thickness of 50 to 70 μm after the processing into a bag shape, And it is preferable that the surface is not water-repellent.

前記接続管が樹脂管であり、前記袋状ろ紙と熱溶着により密着されていることが好ましい。  It is preferable that the connecting pipe is a resin pipe and is in close contact with the bag-like filter paper by heat welding.

前記携行型浄水キットが、さらに、木の葉、ビニール片等の粗大夾雑物を取り除くための粗目フィルタを有することが好ましい。  It is preferable that the portable water purification kit further includes a coarse filter for removing coarse impurities such as leaves and vinyl pieces.

本発明の砂ろ過筒は、ろ過層として石英砂層を有し、該石英砂層が天然の母岩を破砕して得られる破砕石英砂からなり、500〜850μmの粒径のものを重量で全体の50%以上含むことを特徴としている。当該砂ろ過筒は、例えば、ポンプにより送水された被処理水(原水)を膜ろ過器で膜ろ過する簡易浄水装置において、膜ろ過器の前処理手段として用いられる。
また、本発明の他の態様に係る砂ろ過筒は、往復動式手動ポンプなどの吐出脈動を生じるポンプにより送水された被処理水を膜ろ過器で膜ろ過する簡易浄水装置において、前記膜ろ過器の前処理手段として前記ポンプと前記膜ろ過器との間に配置される砂ろ過筒であって、該砂ろ過筒のろ過層の上方に前記ポンプにより送水される被処理水の脈動を低減するための空気層を備えていることを特徴としている。
なお、前記砂ろ過筒は、ろ過時に上方から下方に通水される。
The sand filter cylinder of the present invention has a quartz sand layer as a filtration layer, and the quartz sand layer is made of crushed quartz sand obtained by crushing a natural host rock, and has a particle diameter of 500 to 850 μm as a whole. It is characterized by containing 50% or more. The sand filter cylinder is used, for example, as a pretreatment means of a membrane filter in a simple water purifier that performs membrane filtration of water to be treated (raw water) sent by a pump with a membrane filter.
Further, the sand filter cylinder according to another aspect of the present invention is the simple water purifier for membrane-filtering the treated water fed by a pump that generates discharge pulsation such as a reciprocating manual pump in the membrane filter. A sand filter cylinder disposed between the pump and the membrane filter as pretreatment means for a vessel, and reduces pulsation of water to be treated sent by the pump above the filtration layer of the sand filter cylinder It is characterized by having an air layer to do.
In addition, the said sand filter cylinder is water-passed from upper direction to the downward direction at the time of filtration.

本発明の紙フィルタカートリッジを備えたろ過器は、一端に底部を、他端に開口部を有し、前記底部又は底部近傍にろ過水を取り出す取出し口を有する筒型の容器本体と、前記容器本体内に収容され、平面視略矩形状の扁平な袋状に形成され、一隅に小孔部を有する袋状ろ紙、及び一端が外方に突出するように該小孔部より該袋状ろ紙内に挿入され、該小孔部近傍で密着固定された接続管を有する紙フィルタカートリッジと、前記紙フィルタカートリッジを前記容器本体に収容した際に前記容器本体内に流路となる間隙を形成するための多孔質体からなるシート状のスペーサと、有底筒型で、肉厚の底部に貫通孔を有し、該貫通孔の外方側に内螺子部を有する、前記容器本体の開口部を閉塞する蓋体と、前記内螺子部に螺合可能な外螺子部を一端に備える被処理水を導入する導入管と、を備え、前記ろ過器は、前記蓋体の貫通孔内の内螺子部に、前記導入管を螺合し、該貫通孔の他端側に、前記紙フィルタカートリッジの接続管を挿入することで前記導入管と該接続管を液密に接続し、前記紙フィルタカートリッジを、該紙フィルタカートリッジの袋状ろ紙部に重ね合わせた前記スペーサと共に前記接続管を軸として巻き取った状態で、前記容器本体内に収容し、前記蓋体で該容器本体の開口部を閉塞することで組立てられ、前記導入管から前記接続管を介して前記袋状ろ紙内に被処理水を導入し、該袋状ろ紙を透過したろ過水を前記容器本体底部の取出し口より取り出し、被処理水より取り除いた汚濁物を前記袋状ろ紙内に溜めるようにしたことを特徴としている。  The filter equipped with the paper filter cartridge of the present invention has a cylindrical container body having a bottom at one end, an opening at the other end, and an outlet for taking out filtrated water at or near the bottom. A bag-shaped filter paper housed in the body and formed into a flat bag shape having a substantially rectangular shape in plan view and having a small hole portion at one corner, and the bag-shaped filter paper from the small hole portion so that one end protrudes outward. A paper filter cartridge having a connecting pipe inserted into the small hole and fixed in the vicinity of the small hole, and a gap serving as a flow path is formed in the container body when the paper filter cartridge is accommodated in the container body. An opening of the container main body having a sheet-like spacer made of a porous body, a bottomed cylindrical shape, a through hole in a thick bottom portion, and an inner screw portion on an outer side of the through hole A lid that closes the outer thread and an outer thread that can be screwed into the inner thread. An inlet pipe for introducing the water to be treated provided at the end, and the filter is screwed into the inner screw portion in the through hole of the lid body, and is connected to the other end side of the through hole. The paper tube is connected to the introduction tube and the connection tube in a fluid-tight manner by inserting a connection tube of the paper filter cartridge, and the paper filter cartridge is superposed on the bag-shaped filter paper portion of the paper filter cartridge together with the spacer. In a state where it is wound around the connecting pipe as an axis, it is housed in the container body and assembled by closing the opening of the container body with the lid, and the bag-like shape is formed from the introduction pipe through the connecting pipe. The treated water was introduced into the filter paper, the filtered water that permeated through the bag-shaped filter paper was taken out from the outlet at the bottom of the container body, and the contaminants removed from the treated water were stored in the bag-shaped filter paper. It is characterized by.

本発明の携行型(簡易)浄水装置は、被処理水を汲み上げて送水するポンプと、ろ過層として石英砂層を有する砂ろ過筒と、活性炭を充填した活性炭筒及び/又は膜ろ過器と、前記各構成要素を繋ぐ配管と、を有し、前記膜ろ過器は、精密ろ過膜、限外ろ過膜又は逆浸透膜を備え、前記ポンプ、前記砂ろ過筒、前記活性炭筒及び/又は膜ろ過器の順に、前記配管により各構成要素を連結し、ポンプで汲み上げられる被処理水を砂ろ過筒でろ過した後、活性炭筒及び/又は膜ろ過器に通水し、処理水を得ることを特徴としている。
また、前記携行型浄水装置は、上述の携行用ケース内に収容し得る。
The portable (simple) water purifier of the present invention includes a pump that pumps up and feeds water to be treated, a sand filter cylinder having a quartz sand layer as a filter layer, an activated carbon cylinder and / or a membrane filter filled with activated carbon, And the membrane filter includes a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane, and the pump, the sand filtration tube, the activated carbon tube and / or the membrane filter. In this order, the constituent elements are connected by the pipes, and the treated water pumped up by the pump is filtered through a sand filter cylinder, and then passed through an activated carbon cylinder and / or a membrane filter to obtain treated water. Yes.
Moreover, the said portable water purifier can be accommodated in the above-mentioned carrying case.

本発明によれば、石英砂層をろ過層として備えた砂ろ過筒を、活性炭筒及び/又は膜ろ過器の前段に備えているので、活性炭筒や膜ろ過器の使用期間をより延ばすことが可能となり、システム全体の使用可能な時間を延ばすことができる。
また、他の態様によれば、手動ポンプを用いることで、電気がない状況での使用も可能となり、さらに、ろ過層の上部に空気層を備えた砂ろ過筒を用いることで、手動ポンプにより生じる脈動を低減し、後段の膜ろ過器等にかかる水量負荷を略均一に保持することが可能となる。
また、他の態様によれば、前処理手段(前処理器)として、さらに、使い捨て可能な紙フィルタカートリッジを用いることで、後段の砂ろ過筒にかかる負担を軽減し、システムの使用可能な時間を一層長期化することが可能となる。
According to the present invention, since the sand filter cylinder provided with the quartz sand layer as the filtration layer is provided in the front stage of the activated carbon cylinder and / or the membrane filter, it is possible to further extend the use period of the activated carbon cylinder and the membrane filter. Thus, the usable time of the entire system can be extended.
In addition, according to another aspect, by using a manual pump, it can be used in a situation where there is no electricity, and further, by using a sand filter cylinder having an air layer above the filter layer, The generated pulsation can be reduced, and the water load applied to the subsequent membrane filter or the like can be maintained substantially uniformly.
In addition, according to another aspect, by using a disposable paper filter cartridge as the pretreatment means (pretreatment device), the burden on the subsequent sand filter cylinder is reduced, and the system usable time is reduced. Can be further prolonged.

図1は、本発明の携行型浄水キットの一使用態様を説明するための模式図である。  FIG. 1 is a schematic view for explaining one usage mode of the portable water purification kit of the present invention. 図2は、紙フィルタカートリッジを備えたろ過器の構造を説明するための一部を切欠いた斜視図である。  FIG. 2 is a perspective view with a part cut away for explaining the structure of a filter provided with a paper filter cartridge. 図3は、紙フィルタカートリッジを備えたろ過器の構造を説明するための断面図である。  FIG. 3 is a cross-sectional view for explaining the structure of a filter provided with a paper filter cartridge. 図4(a)は、ろ過器に収容される前の紙フィルタカートリッジの構造を説明するための斜視図であり、図4(b)は、ろ過器に収容する際の紙フィルタカートリッジの巻き取り状態を説明するための一部を切欠いた斜視図である。  FIG. 4A is a perspective view for explaining the structure of the paper filter cartridge before being accommodated in the filter, and FIG. 4B is the winding of the paper filter cartridge when being accommodated in the filter. It is the perspective view which notched a part for explaining a state. 図5は、一実施形態に係る砂ろ過筒を説明するための概略断面図である。  FIG. 5 is a schematic cross-sectional view for explaining a sand filter cylinder according to an embodiment. 図6は、本発明に用いられる往復動式手動ポンプの模式図である。  FIG. 6 is a schematic view of a reciprocating manual pump used in the present invention.

本発明の携行型浄水キットは、被処理水を汲み上げて送水するポンプと、砂ろ過筒と、活性炭筒及び/又は膜ろ過器とを含み構成されている。本発明の携行型浄水キットは、必要に応じて、粗目フィルタ、紙フィルタカートリッジを備えたろ過器(以下、単に紙フィルタともいう)等を含んでもよく、また、各ユニット(ポンプ、砂ろ過筒、活性炭筒、膜ろ過器、粗目フィルタ、紙フィルタ等)間を連結する可撓性を有するホース状の配管を含んでいてもよい。  The portable water purification kit of the present invention includes a pump that pumps up and feeds water to be treated, a sand filter cylinder, an activated carbon cylinder and / or a membrane filter. The portable water purification kit of the present invention may include a filter equipped with a coarse filter and a paper filter cartridge (hereinafter also simply referred to as a paper filter), etc., as required, and each unit (pump, sand filter cylinder). , An activated carbon cylinder, a membrane filter, a coarse filter, a paper filter, and the like) may be included.

本発明の携行型浄水キットでは、活性炭筒及び/又は膜ろ過器の前に、砂ろ過筒を配置して、ポンプで汲み上げた被処理水を一旦砂ろ過筒で処理した後に活性炭筒及び/又は膜ろ過器で処理する。また、粗目フィルタ又は紙フィルタを用いる場合には、粗目フィルタ又は紙フィルタは、砂ろ過筒の前段に配置され、粗目フィルタ及び紙フィルタの双方を用いる場合は、粗目フィルタ、紙フィルタ、砂ろ過筒、活性炭筒、膜ろ過器の順で設置される。なお、活性炭筒及び膜ろ過器は、両方設置してもよいが、いずれか一方のみを配置してもよい。このような携行型浄水キットを構成する各ユニット(ポンプを含む)は、上記順序で、例えば可撓性を有するホースにより連結される。  In the portable water purification kit of the present invention, a sand filter cylinder is disposed in front of the activated carbon cylinder and / or the membrane filter, and the treated water pumped up by the pump is once treated with the sand filter cylinder and then the activated carbon cylinder and / or Treat with membrane filter. Further, when a coarse filter or a paper filter is used, the coarse filter or the paper filter is disposed in the front stage of the sand filter cylinder. When both the coarse filter and the paper filter are used, the coarse filter, the paper filter, and the sand filter cylinder are used. It is installed in the order of activated carbon cylinder and membrane filter. In addition, although both an activated carbon cylinder and a membrane filter may be installed, you may arrange | position only any one. Each unit (including a pump) constituting such a portable water purification kit is connected in the above order, for example, by a flexible hose.

本発明の携行型キットで浄水化し得る被処理水は、緊急時に飲料水化処理可能な水であれば特に限定されず、例えば、人工池、プール、池、湖沼、小川、浴槽等の水が挙げられる。  The treated water that can be purified with the portable kit of the present invention is not particularly limited as long as it is water that can be used for drinking water in an emergency. For example, water such as artificial ponds, pools, ponds, lakes, streams, and bathtubs can be used. Can be mentioned.

以下に、携行型浄水キットの主な構成要素について順次説明する。
本発明で用いられるポンプは、被処理水を汲み上げて送水することが可能であれば特に限定されず、電動式であっても手動式であってもよい。但し、災害時や屋外で使用する場合には、適当な電源が得られない可能性も高く、そのような用途に使用する場合には、手動式(例えば往復動式手動ポンプ)を備えていることが好ましい。往復動式ポンプ(いわゆる往復ポンプ)は、シリンダ(筒)内をピストンまたはプランジャが往復して、シリンダ内の容積を変えることにより、液体を吸い込み、送り出す構造を有するポンプである。具体的には、例えば特許文献1に記載の往復動式手動ポンプを用いることができる。
Below, the main components of the portable water purification kit will be described sequentially.
The pump used in the present invention is not particularly limited as long as it can pump up and feed water to be treated, and may be electric or manual. However, when used in a disaster or outdoors, there is a high possibility that an appropriate power source cannot be obtained. When used in such applications, a manual type (for example, a reciprocating manual pump) is provided. It is preferable. A reciprocating pump (so-called reciprocating pump) is a pump having a structure in which a piston or plunger reciprocates in a cylinder (cylinder) to change the volume in the cylinder, thereby sucking and sending liquid. Specifically, for example, a reciprocating manual pump described in Patent Document 1 can be used.

本発明で用いられる砂ろ過筒は、ろ過材として石英砂を使用していることが好ましい。石英砂は、天然に産出するものを使用してもよく、珪石等の天然の母岩を破砕したものを使用してもよいが、粉砕物を用いた方がろ過層全体で懸濁物を捕捉し得るので好ましい。また、石英砂は、500〜850μmの粒径のものを重量で全体の50%以上、好ましくは60〜90%程度含むことが望ましい。このような石英砂を用いると、砂ろ過筒、及び、後段の活性炭筒及び膜ろ過器が一層長期に亘り目詰まりを起こし難くなる。また、砂ろ過筒内に充填されたろ過砂は、水洗により容易に再生可能である。砂ろ過筒内のろ過層の上部には、空気層が設けられていることが好ましい。空気層を設けておくことにより、手動ポンプ等の脈動を低減し得ると共に、手動ポンプ操作時に作業員にかかる負荷を軽減することが可能となる。  The sand filter cylinder used in the present invention preferably uses quartz sand as a filter medium. Quartz sand may be naturally produced or crushed natural host rock such as silica stone, but the pulverized material will cause suspension throughout the filtration layer. It is preferable because it can be captured. Further, it is desirable that the quartz sand contains particles having a particle diameter of 500 to 850 μm by weight of 50% or more, preferably about 60 to 90%. When such quartz sand is used, the sand filter cylinder, the activated carbon cylinder and the membrane filter in the subsequent stage are less likely to be clogged for a longer period of time. Moreover, the filter sand filled in the sand filter cylinder can be easily regenerated by washing with water. It is preferable that an air layer is provided above the filtration layer in the sand filter cylinder. By providing the air layer, it is possible to reduce the pulsation of the manual pump and the like, and it is possible to reduce the load on the worker when operating the manual pump.

本発明で用いられる活性炭筒は、略円筒形状の容器に活性炭を充填したものが好適に用いられ、特に、装填される活性炭をカートリッジ方式としたものであると、災害時等の緊急時の取扱い容易性の点から好ましい。  The activated carbon cylinder used in the present invention is preferably used in a substantially cylindrical container filled with activated carbon, especially when the loaded activated carbon is a cartridge system, handling in an emergency such as a disaster. It is preferable from the viewpoint of ease.

本発明で用いられる膜ろ過器は、携行可能なものであれば特に限定されないが、外形が略円筒状のものであると、携行時の収納のし易さ等の観点から好ましい。また、膜ろ過器のろ過膜は、精密ろ過膜(MF膜)、限外ろ過膜(UF膜)、ナノろ過膜(NF膜)、又は逆浸透膜のいずれであってもよいが、手動ポンプの操作にかかる負荷労力が少ないという点からはMF膜又はUF膜が好ましい。  The membrane filter used in the present invention is not particularly limited as long as it can be carried. However, it is preferable that the outer shape is substantially cylindrical from the viewpoint of ease of storage during carrying. The filtration membrane of the membrane filter may be a microfiltration membrane (MF membrane), an ultrafiltration membrane (UF membrane), a nanofiltration membrane (NF membrane), or a reverse osmosis membrane, but a manual pump The MF membrane or the UF membrane is preferable from the viewpoint that the load labor required for the operation is small.

また、砂ろ過筒の前段に必要に応じて紙フィルタを用いてもよい。紙フィルタは、例えば0.05〜1mm程度の小粒子を捕捉するためのもので、砂ろ過筒にかかる負荷を低減し得る。また、カートリッジ式とすることで交換が容易で使い捨てすることができ、砂ろ過筒のろ過層の洗浄再生回数を減らして長時間の使用を可能とするので、災害時等の緊急時の取扱いの容易性の点で好ましい。  Moreover, you may use a paper filter for the front | former stage of a sand filter cylinder as needed. The paper filter is for capturing small particles of about 0.05 to 1 mm, for example, and can reduce the load on the sand filter cylinder. In addition, the cartridge type is easy to replace and disposable, and the sand filter can be used for a long time by reducing the number of times of cleaning and cleaning the filtration layer. It is preferable in terms of ease.

さらに、砂ろ過筒の前段(紙フィルタを設置する場合は、紙フィルタの前段)に、木の葉やビニール片等の粗大夾雑物が砂ろ過筒へ流入するのを阻止するための粗目フィルタを設置してもよい。粗目フィルタは、粗大夾雑物を除去し得るものであれば特に限定されず、網状体、多数の開口部(小孔、スリット等)を有する成形体等のいずれであってもよく、目開きは、例えば、1mmより大きく、好ましくは、2〜5mm程度のものが用いられる。粗目フィルタの形状も、特に限定されないが、例えば円筒状であると携行の際、スペースをとらないので便利である。また、粗目フィルタの素材は、樹脂材料、金属材料等のいずれであってもよいが携行時の軽量化を考慮し樹脂材料が好ましい。  In addition, a coarse filter is installed in front of the sand filter cylinder (in the case of installing a paper filter, in front of the paper filter) to prevent coarse impurities such as leaves and vinyl pieces from flowing into the sand filter cylinder. May be. The coarse filter is not particularly limited as long as coarse impurities can be removed, and may be any of a net-like body, a molded body having a large number of openings (small holes, slits, etc.), and the opening is For example, those larger than 1 mm, preferably about 2 to 5 mm are used. The shape of the coarse filter is not particularly limited. For example, a cylindrical filter is convenient because it does not take up space when being carried. The material of the coarse filter may be a resin material, a metal material, or the like, but a resin material is preferable in consideration of weight reduction during carrying.

以下、図面を参照しながら本発明について、より詳細に説明する。
図1は、本発明の携行型浄水キットの一使用態様を説明するための模式図である。
図1に示すように、本実施形態の携行型浄水キットは、粗目フィルタ2、紙フィルタカートリッジ407を備えたろ過器4、往復動式手動ポンプ5(以下、単に手動ポンプともいう)、砂ろ過筒6、活性炭筒7、及び膜ろ過器8から主に構成されており、これらのユニットを必要に応じて備えられるホース状の配管(ラインL1〜L6)により当該順に連結することで、簡易浄水装置(小型浄水装置)100が構築される。
Hereinafter, the present invention will be described in more detail with reference to the drawings.
FIG. 1 is a schematic view for explaining one usage mode of the portable water purification kit of the present invention.
As shown in FIG. 1, the portable water purification kit of this embodiment includes a coarse filter 2, a filter 4 having a paper filter cartridge 407, a reciprocating manual pump 5 (hereinafter also simply referred to as a manual pump), sand filtration. It is mainly composed of the cylinder 6, the activated carbon cylinder 7, and the membrane filter 8, and simple water purification by connecting these units in this order by hose-like piping (lines L1 to L6) provided as necessary. A device (small water purification device) 100 is constructed.

原水(被処理水)10が貯留された水槽1内には、樹脂製の粗目フィルタ2が、水槽1内の底泥等を吸い上げないように、水面上に浮かべた直径7cm発泡スチロール製の球状フロート(浮子)3に吊り下げて設置されている。
粗目フィルタ2は、5mm径の複数の穴が穿たれた、直径10cm、長さ17cmの略円筒形状をした樹脂製の筒体で、原水に含まれる木の葉、枝、ビニール片等の大きな夾雑物を除去する。
In the water tank 1 in which the raw water (treated water) 10 is stored, a spherical float made of 7 cm diameter polystyrene floated on the surface of the water so that the coarse filter 2 made of resin does not suck up the bottom mud and the like in the water tank 1. (Float) 3 is hung and installed.
The coarse filter 2 is a resin cylinder having a substantially cylindrical shape with a diameter of 10 cm and a length of 17 cm, in which a plurality of holes with a diameter of 5 mm are formed, and large contaminants such as leaves, branches, and vinyl pieces contained in the raw water. Remove.

手動ポンプ5を稼働すると、手動ポンプ5の吸引側に配設されたこの粗目フィルタ2を介して被処理水が吸引され、圧力計11を備えたラインL1を経てろ過器4に送水される。  When the manual pump 5 is operated, the water to be treated is sucked through the coarse filter 2 disposed on the suction side of the manual pump 5 and is sent to the filter 4 through the line L1 provided with the pressure gauge 11.

ろ過器4には、内部に紙フィルタカートリッジが備えられており、紙フィルタカートリッジを通過した水が、ラインL2、手動ポンプ5を介し、ラインL3を経て、砂ろ過筒6に移送される。ラインL3には、流量調整用のバルブ12及び圧力計13が備えられており、手動ポンプ5から吐出された吐出水は、バルブ12により流量が調整された状態で砂ろ過筒6に送られ、砂ろ過筒6で殆どの懸濁物質が捕捉される。  The filter 4 is provided with a paper filter cartridge inside, and the water that has passed through the paper filter cartridge is transferred to the sand filter cylinder 6 via the line L2 and the manual pump 5 via the line L3. The line L3 is provided with a valve 12 for adjusting the flow rate and a pressure gauge 13, and the discharge water discharged from the manual pump 5 is sent to the sand filter cylinder 6 with the flow rate adjusted by the valve 12, Most suspended solids are captured by the sand filter cylinder 6.

砂ろ過筒6より得られる濾過水は、圧力計14を備えたラインL4を介して活性炭筒7に送られる。活性炭筒7では、主に色度成分及び臭気成分が除去される。その後、さらに圧力計15を有するラインL5を介して膜ろ過器8に送水され、他の処理では除去しきれなかった成分(一般細菌、大腸菌等を含む)が除去される。最終的に得られる処理水は流量計16を備えたラインL6を介して飲料水貯槽9に貯留され、飲料水として飲用される。  The filtered water obtained from the sand filter cylinder 6 is sent to the activated carbon cylinder 7 through a line L4 provided with a pressure gauge 14. In the activated carbon cylinder 7, chromaticity components and odor components are mainly removed. Thereafter, water is further sent to the membrane filter 8 via the line L5 having the pressure gauge 15, and components (including general bacteria, E. coli, etc.) that could not be removed by other processes are removed. The treated water finally obtained is stored in the drinking water storage tank 9 via the line L6 provided with the flow meter 16, and is drunk as drinking water.

圧力計11、13、14、15は、それぞれろ過器4、砂ろ過筒6、活性炭筒7及び膜ろ過器8の前に設置されており、目詰まりによる異常な圧力上昇が検知された時はそれぞれの機器を洗浄再生又は充填部材を交換することになる。具体的には、ろ過器4の場合は後述する紙フィルタカートリッジ407の交換、砂ろ過筒6の場合はバケツ等に石英砂を移し、水で2〜3回程度撹拌しながら洗浄することによる再生、活性炭筒7及び膜ろ過器8の場合は膜カートリッジの交換となる。なお、圧力計11、13、14、15は、持ち運び途中や現場設置の際にガラスが破損すると危険なため、ガラス素材を使用しないブルドン管式が好適に用いられる。  The pressure gauges 11, 13, 14, and 15 are installed in front of the filter 4, the sand filter cylinder 6, the activated carbon cylinder 7 and the membrane filter 8, respectively, and when an abnormal pressure increase due to clogging is detected. Each device is cleaned and replaced or the filling member is replaced. Specifically, in the case of the filter 4, replacement by a paper filter cartridge 407 to be described later, in the case of the sand filter cylinder 6, the quartz sand is transferred to a bucket or the like, and the regeneration is performed by washing with water about 2 to 3 times. In the case of the activated carbon cylinder 7 and the membrane filter 8, the membrane cartridge is replaced. In addition, since the pressure gauges 11, 13, 14, and 15 are dangerous when the glass is broken during carrying or on-site installation, a Bourdon tube type that does not use a glass material is preferably used.

流量計16は、簡易浄水装置全体の毎分当たりの浄水量を測定するもので、例えば電磁流量計が用いられる。なお、実現場では流量計16はなくても、浄化した飲料水の量をバケツの目盛り等で大まかに確認ができればそれで十分である。  The flow meter 16 measures the amount of purified water per minute of the entire simple water purifier, and for example, an electromagnetic flow meter is used. Even if there is no flow meter 16 at the realization site, it is sufficient if the amount of purified drinking water can be roughly confirmed with a bucket scale or the like.

次に、紙フィルタカートリッジを備えたろ過器4の一例について、図2乃至図4を参照しながら説明する。
図2は、ろ過器4の構造を説明するための一部を切欠いた斜視図である。図3は、ろ過器4の構造を説明するための断面図である。また、図4(a)は、ろ過器4に収容される前の紙フィルタカートリッジの構造を説明するための斜視図であり、図4(b)は、ろ過器4に収容する際の紙フィルタカートリッジの巻き取り状態を説明するための一部を切欠いた斜視図である。
Next, an example of the filter 4 provided with the paper filter cartridge will be described with reference to FIGS.
FIG. 2 is a perspective view with a part cut away for explaining the structure of the filter 4. FIG. 3 is a cross-sectional view for explaining the structure of the filter 4. 4A is a perspective view for explaining the structure of the paper filter cartridge before being accommodated in the filter 4, and FIG. 4B is a paper filter when being accommodated in the filter 4. It is the perspective view which notched a part for explaining the winding state of a cartridge.

図2及び図3に示されるように、ろ過器4は、一端が閉塞され、他端が開口された筒状の容器本体401と、容器本体401に収容される紙フィルタカートリッジ407と、容器本体401の開口部411を覆う蓋体403とから主に構成されている。また、紙フィルタカートリッジ407は、袋状ろ紙402及び接続管422から主に構成されている。  As shown in FIGS. 2 and 3, the filter 4 includes a cylindrical container body 401 whose one end is closed and the other end is opened, a paper filter cartridge 407 accommodated in the container body 401, and a container body. The lid 403 mainly covers the opening 411 of 401. The paper filter cartridge 407 is mainly composed of a bag-shaped filter paper 402 and a connecting pipe 422.

袋状ろ紙402は、一隅に小孔部421を有する平面視略矩形状の扁平な袋体で、小孔部421には、袋状ろ紙402内に被処理水を取り入れるための接続管422が袋状ろ紙402の一辺に沿って挿入されており、この接続管422は、一端側が小孔部421より突出した状態で小孔部421に密着固定されている。接続管422の突出した側には、先端付近にO−リング423が取り付けられており、後述する蓋体403の貫通孔433に挿入された際の貫通孔433との密着性を高め、シール性を向上させている。接続管422の挿入部の長さは、特に限定するものではないが、袋状ろ紙402を巻き取る際に巻き取りがし易くかつ接続管422より導入される水流で袋状ろ紙402が劣化するのを防止するという観点から、近接する袋状ろ紙402の辺の約1/4〜3/4程度であることが好ましい。  The bag-shaped filter paper 402 is a flat bag body having a rectangular shape in a plan view having a small hole portion 421 at one corner. The small hole portion 421 has a connecting pipe 422 for taking in water to be treated into the bag-shaped filter paper 402. The connecting tube 422 is inserted along one side of the bag-shaped filter paper 402, and is firmly fixed to the small hole portion 421 with one end projecting from the small hole portion 421. An O-ring 423 is attached to the protruding side of the connecting pipe 422 near the tip, which improves the adhesion with the through-hole 433 when inserted into the through-hole 433 of the lid 403, which will be described later, and has a sealing property. Has improved. The length of the insertion portion of the connecting pipe 422 is not particularly limited, but the bag-like filter paper 402 is easily wound when the bag-like filter paper 402 is wound, and the bag-like filter paper 402 is deteriorated by the water flow introduced from the connecting pipe 422. From the viewpoint of preventing this, it is preferably about 1/4 to 3/4 of the side of the adjacent bag-shaped filter paper 402.

また、実用性の観点から種々の検討を行った結果、下記条件を満たす素材が好ましいことが判明した。
第一の条件は、撥水処理をしていない素材であることが好ましい。撥水処理を行っている素材に比べ、ろ過速度が向上し得る。
第二の条件は、パルプ100%の素材ではなく、パルプとPET等の合成樹脂材料との混繊維、特にパルプとPETが約1対1の比率(重量比)で含まれる混繊維であることが好ましい。合成樹脂材料が含まれると強度が向上し、また、特にパルプとPETの1対1混繊維であると、切断強度が増す点で好ましい。また、PET等の合成樹脂材料との混繊維にすることで熱溶着ができるため、袋状に形成したり、接続管422を固定したりする際の加工等が容易になる。
第三の条件は、熱ロールによる加熱・加圧処理を行っていることが好ましい。袋状ろ紙402に熱ロールによる加熱・加圧処理が施されていると、ろ過速度を抑止する混繊維の毛羽立ちを低減し得るので、ろ過速度を向上し得る。
第四の条件は、熱ロールによる処理後の袋状ろ紙402の厚さが、50〜70μm程度であることが好ましい。袋状ろ紙402の厚さが上記範囲にあると、嵩張りがなくろ過器4をコンパクトにし得るので携行に便利であると共に、十分なろ可能を保持しつつろ過抵抗を低減することが可能となる。
第五の条件は、袋状ろ紙402の目付けが、20〜40g/m程度であることが好ましい。目付けが上記範囲にあると、ろ過速度と懸濁物質除去性のバランスに優れる。
Further, as a result of various studies from the viewpoint of practicality, it has been found that a material satisfying the following conditions is preferable.
The first condition is preferably a material not subjected to water repellent treatment. The filtration rate can be improved compared to a material subjected to water repellent treatment.
The second condition is not a 100% pulp material but a mixed fiber of pulp and synthetic resin material such as PET, in particular, a mixed fiber containing pulp and PET in a ratio of 1 to 1 (weight ratio). Is preferred. When a synthetic resin material is included, the strength is improved. In particular, a one-to-one mixed fiber of pulp and PET is preferable in terms of increasing the cutting strength. In addition, since heat welding can be performed by using a mixed fiber with a synthetic resin material such as PET, processing or the like when forming a bag or fixing the connecting pipe 422 is facilitated.
As the third condition, it is preferable to perform a heating / pressurizing treatment with a hot roll. When the bag-like filter paper 402 is heated and pressurized with a hot roll, the fuzz of the mixed fiber that suppresses the filtration rate can be reduced, and thus the filtration rate can be improved.
As for 4th conditions, it is preferable that the thickness of the bag-shaped filter paper 402 after the process by a hot roll is about 50-70 micrometers. When the thickness of the bag-shaped filter paper 402 is in the above range, the filter 4 can be made compact without being bulky, so that it is convenient to carry and the filtration resistance can be reduced while maintaining sufficient filterability. .
The fifth condition is that the basis weight of the bag-shaped filter paper 402 is preferably about 20 to 40 g / m 2 . When the basis weight is in the above range, the balance between the filtration rate and the suspended matter removal property is excellent.

このような袋状ろ紙402は、例えば、上記条件を満たす素材からなる略矩形状のろ紙を2枚重ね合わせ、四辺を熱溶着し、袋状にした後、一隅を切欠いて小孔部(切欠き部)421を設け、この小孔部421に樹脂製の接続管422を挿入し、その後、袋状ろ紙402の小孔部421近傍を加熱して袋状ろ紙402と接続管422を熱溶着することで製造し得る。  For example, such bag-shaped filter paper 402 is formed by stacking two substantially rectangular filter papers made of a material satisfying the above conditions, heat-welding four sides, forming a bag shape, and then cutting out one corner to form a small hole (cut (Notch part) 421 is provided, and a resin connection pipe 422 is inserted into the small hole part 421, and then the vicinity of the small hole part 421 of the bag-shaped filter paper 402 is heated to thermally weld the bag-shaped filter paper 402 and the connection pipe 422. Can be manufactured.

袋状ろ紙402は、広げた状態(図4(a)参照)で不織布405上に重ね合わせられ、図4(b)に示すように接続管422を軸として不織布405と共に渦巻き(スパイラル)状に巻き取った巻取体406とした状態で容器本体401内に収容される(図2及び図3参照)。このように、不織布405と袋状ろ紙402を同時に巻き取った巻取体406とすることで、袋状ろ紙402内に被処理水が導入され、袋状ろ紙402が膨化した際にも、巻き取った袋状ろ紙402同士或いは袋状ろ紙402と容器本体401内壁とが接触することで、容器本体401内に処理水が通過する流路となる隙間がなくなり、袋状ろ紙402を透過した処理水の流れに支障をきたすのを回避することが可能となる。
不織布405の厚さは、あまり厚いと嵩張り、ろ過器4が大きくなるので携行に不向きであり、また、薄すぎると適正な水路(処理水流路)を袋状ろ紙402間に形成し得なくなる。したがって厚さは2〜5mm程度であることが好ましい。
The bag-shaped filter paper 402 is overlaid on the nonwoven fabric 405 in an unfolded state (see FIG. 4A), and is spirally formed with the nonwoven fabric 405 around the connection tube 422 as shown in FIG. 4B. The wound body 406 is wound and accommodated in the container body 401 (see FIGS. 2 and 3). In this way, by forming the wound body 406 by winding the nonwoven fabric 405 and the bag-shaped filter paper 402 at the same time, even when the water to be treated is introduced into the bag-shaped filter paper 402 and the bag-shaped filter paper 402 expands, The bag-shaped filter papers 402 taken together or the bag-shaped filter paper 402 and the inner wall of the container main body 401 come into contact with each other, so that there is no gap in the container main body 401 serving as a flow path through which treated water passes, and the bag-shaped filter paper 402 is permeated. It is possible to avoid obstructing the flow of water.
If the thickness of the nonwoven fabric 405 is too thick, the nonwoven fabric 405 is bulky and is unsuitable for carrying because the filter 4 becomes large. If it is too thin, an appropriate water channel (treated water channel) cannot be formed between the bag-shaped filter papers 402. . Therefore, the thickness is preferably about 2 to 5 mm.

蓋体403は、肉厚の底部431を有する筒体で、筒部432の内径は容器本体401の開口部411側に外嵌し得るように容器本体401の外径より若干大きく形成されている。容器本体401の開口部411近傍の外壁には外螺子部412が設けられており、この外螺子部412に螺合し得るよう、蓋体403の筒部432の内壁には内螺子部(符号なし)が設けられている。また、外螺子部412の終端部にはO−リング413が取り付けられており、蓋体403とのシール性を高めている。底部431には、貫通孔433が設けられており、貫通孔433の外方側(容器本体401に面する側と反対側)には貫通孔433の長さ方向で半ば位まで内螺子部434が設けられ、導入管404の外螺子部441と螺合可能にされている。導入管404の外螺子部441の終端部分には、導入管404を螺合した際、蓋体403に圧接されるO−リング442が装着されており、容器本体401内からの水漏れを一層確実に防止することが可能となっている。貫通孔433の容器本体401と対向する側には、先端付近にO−リング423が取り付けられた接続管422が挿入され、貫通孔433内で同軸上に導入管404と接続管422が液密に接続される。  The lid body 403 is a cylindrical body having a thick bottom part 431, and the inner diameter of the cylindrical part 432 is slightly larger than the outer diameter of the container main body 401 so that it can be fitted on the opening 411 side of the container main body 401. . An outer screw portion 412 is provided on the outer wall in the vicinity of the opening 411 of the container body 401, and an inner screw portion (reference number) is provided on the inner wall of the cylindrical portion 432 of the lid 403 so that the outer screw portion 412 can be screwed. None) is provided. In addition, an O-ring 413 is attached to the end portion of the external screw portion 412 to enhance the sealing performance with the lid body 403. The bottom portion 431 is provided with a through hole 433, and an inner screw portion 434 is provided on the outer side of the through hole 433 (on the side opposite to the side facing the container body 401) in the length direction of the through hole 433 to the middle position. Is provided so that it can be screwed into the outer screw portion 441 of the introduction tube 404. An O-ring 442 that is in pressure contact with the lid 403 when the introduction tube 404 is screwed is attached to the end portion of the outer screw portion 441 of the introduction tube 404, thereby further preventing water leakage from inside the container body 401. It can be reliably prevented. A connecting pipe 422 with an O-ring 423 attached in the vicinity of the tip is inserted on the side of the through hole 433 facing the container body 401, and the introduction pipe 404 and the connecting pipe 422 are coaxially placed in the through hole 433. Connected to.

導入管404は、内部に貫通孔443を有し、蓋体403との接続側と反対側がラインL1と接続されており、L1を介して導入管404に導入された被処理水は、接続管422を介して袋状ろ紙402内に導入され、袋状ろ紙402を透過したろ過水は、スペーサとしての不織布405内(及び容器本体401内の間隙)を通過し、容器本体401の底部414に設けられた取出し口415より取り出される。その際、袋状ろ紙402内には、被処理水より取り除かれた汚物が溜まることになる。  The introduction pipe 404 has a through hole 443 inside, and the side opposite to the connection side with the lid body 403 is connected to the line L1, and the water to be treated introduced into the introduction pipe 404 via the L1 is connected to the connection pipe. The filtered water introduced into the bag-shaped filter paper 402 via 422 and permeated through the bag-shaped filter paper 402 passes through the non-woven fabric 405 as a spacer (and the gap in the container main body 401), and reaches the bottom 414 of the container main body 401. It is taken out from the provided outlet 415. At that time, the filth removed from the water to be treated is accumulated in the bag-shaped filter paper 402.

袋状ろ紙402内に汚物が増えたり、或いは目詰まり等して袋状ろ紙402のろ過能が低下した際には、袋状ろ紙402と先端部にO−リング423が密着した接続管422とが一体となった紙フィルタカートリッジ407を交換する。紙フィルタカートリッジ407は、上述のとおり、蓋体403の貫通孔433に接続管422を挿入することで装着されているので、接続管422を引き抜くことで容易に取り外し可能であり、使い終わった紙フィルタカートリッジ407は袋状ろ紙402内に溜まった汚物と共にそのまま廃棄することができる。また、新たな紙フィルタカートリッジ407も同様に蓋体403の貫通孔433に挿入することで装着し得る。したがって、災害時等の非常時においても、手を汚さずに煩雑な操作なしに紙フィルタカートリッジ407の交換が可能であるので好ましい。  When filth increases in the bag-like filter paper 402 or clogging or the like, and the filtration performance of the bag-like filter paper 402 is reduced, the bag-like filter paper 402 and the connecting pipe 422 with the O-ring 423 closely attached to the tip portion Is replaced with the paper filter cartridge 407 integrated. Since the paper filter cartridge 407 is mounted by inserting the connection tube 422 into the through hole 433 of the lid 403 as described above, the paper filter cartridge 407 can be easily removed by pulling out the connection tube 422. The filter cartridge 407 can be discarded as it is together with the dirt accumulated in the bag-like filter paper 402. Similarly, a new paper filter cartridge 407 can be mounted by being inserted into the through hole 433 of the lid 403. Therefore, it is preferable because the paper filter cartridge 407 can be replaced without complicated operations even in an emergency such as a disaster.

このように紙フィルタカートリッジ407の交換は容易であるが、紙フィルタカートリッジ407を長時間利用可能とするために、紙フィルタカートリッジ407の線束(LV)は、5〜15m/m/日程度とすることが好ましい。Thus, the replacement of the paper filter cartridge 407 is easy, but in order to make the paper filter cartridge 407 usable for a long time, the line bundle (LV) of the paper filter cartridge 407 is about 5 to 15 m 3 / m 2 / day. It is preferable that

次に、本実施形態に用いられる砂ろ過筒6について説明する。
図5は、一実施形態に係る砂ろ過筒6を説明するための概略断面図である。
図5に示すように、砂ろ過筒6は、後述するろ過層を有する有底円筒状の砂ろ過容器601と砂ろ過容器601の開口端を閉塞する蓋体611とから主に構成されている。
砂ろ過容器601内には、ろ過層として、下から順に支持床としての樹脂ペレット層602、下部不織布層603、石英砂層604、上部不織布層605、空気層(クッション部)606が形成されている。
Next, the sand filter cylinder 6 used for this embodiment is demonstrated.
FIG. 5 is a schematic cross-sectional view for explaining a sand filter cylinder 6 according to an embodiment.
As shown in FIG. 5, the sand filtration cylinder 6 is mainly composed of a bottomed cylindrical sand filtration container 601 having a filtration layer, which will be described later, and a lid 611 that closes the open end of the sand filtration container 601. .
In the sand filtration container 601, a resin pellet layer 602 as a support floor, a lower nonwoven fabric layer 603, a quartz sand layer 604, an upper nonwoven fabric layer 605, and an air layer (cushion portion) 606 are formed in order from the bottom as a filtration layer. .

砂ろ過筒6の水面積当たりのLVは、3〜6m/m/時程度であることが好ましく、砂ろ過筒6の容積当たりの浄水速度すなわち容積速度(SV)は30〜50m/m/時程度であることが好ましい。LV及びSVが上記範囲にあると、懸濁物の除去性、脈動防止、適正設計条件の設定に優れる。The LV per water area of the sand filter cylinder 6 is preferably about 3 to 6 m 3 / m 2 / hour, and the water purification speed per volume of the sand filter cylinder 6, that is, the volume speed (SV) is 30 to 50 m 3 / It is preferably about m 3 / hour. When LV and SV are in the above ranges, it is excellent in suspension removability, pulsation prevention, and setting of appropriate design conditions.

以下、砂ろ過筒6を構成する要素について順に説明する。
最上部の空気層606は、往復動作式の手動ポンプ5の脈動を抑えるもので、この空気層606の容積は、簡易浄水装置100を、4〜5時間程度運転すると、一部の空気が被処理水に同伴されて後段に運ばれ、空気層の減少分を被処理水が満たすこととなるため、その影響で半分程度に減少する。そのため、常時空気層606を一定以上に保持するために、蓋体611に砂ろ過筒6の上部の空気層606に連通するように空気取り入れ口として、外気に連なる空気取り入れバルブ607を備えた配管(空気取り入れ管)608を設けており、同時に過剰水を排除し、水位を下げて水面位置を所定位置に調整するための排出口として、水位調整バルブ609を備えた配管(排水管)610を設けている。
Hereinafter, the elements constituting the sand filter cylinder 6 will be described in order.
The uppermost air layer 606 suppresses the pulsation of the reciprocating manual pump 5, and the volume of the air layer 606 is such that when the simple water purifier 100 is operated for about 4 to 5 hours, a part of the air is covered. The water to be treated is transported to the subsequent stage and the treated water fills the decrease in the air layer. Therefore, in order to always keep the air layer 606 above a certain level, a pipe provided with an air intake valve 607 connected to the outside air as an air intake port so as to communicate with the air layer 606 on the upper part of the sand filter cylinder 6 with the lid 611. (Air intake pipe) 608 is provided, and at the same time, a pipe (drain pipe) 610 provided with a water level adjustment valve 609 is used as an outlet for removing excess water and lowering the water level to adjust the water surface position to a predetermined position. Provided.

蓋体611には、被処理水の導入口(図示略)が外方に突設されており、ラインL3と液密に接続可能にされている。蓋体611は、凹状で、内底616には内底外縁に沿って浅溝617が形成され、パッキン618が詰められており、砂ろ過容器601を閉塞する際に、砂ろ過器601の開口端とパッキン618を接触させることでシール性を高めている。蓋体611の内底616の導入口の直下には、ラインL3より流入する被処理水の勢いを止め、ろ過層上にある程度分散させて供給するために、内底616と若干距離を開けた位置に散水板612が2本の丸棒613により固定されている。蓋体611、散水板612及び丸棒613が塩化ビニール等の樹脂製である場合には、蓋体611及び散水板612と丸棒613とは、例えば溶着又は接着により固定される。散水板612は、ラインL3を構成する配管の内径より2〜10倍程度大きな径の円盤状で、砂ろ過容器601の内径の1/3〜1/5程度であることが好ましい。散水板612の直径を、砂ろ過容器601の内面積をカバーし得る大きさとし、散水板にパンチング穴等を設けて、砂ろ過容器601のろ過層の表面全域に散水することも考えられるが、現場の設置状況は不明で、むしろ水平設置が難しい場合が多く、散水板が傾いて設置されると一方向に限定された流れとなり、全体に散水されなくなるため、携行用として使用する場合には、散水板612を大きくするのはむしろ好ましくない。一方、散水板612がないか或いは小さすぎる場合は、ラインL3から流入する被処理水の勢いで石英砂層604の中心部が凹み、逆円錐形の穴が形成され、水の短絡が起こり易くなる。小さな携帯用の砂ろ過筒6では、コンパクト性や重量低減が重要なポイントになるため充填容積も高さも大きくできない。石英砂の充填高さ(石英砂層604の高さ)は、4〜10cm程度が好ましいが、このような高さで深さ2〜3cm程度の凹みが生じると、短絡が生じる可能性が大き過ぎる。したがって、携帯用では、散水板612を設置することが望ましい。L3を構成する配管を、砂ろ過筒6に入る前に、複数の配管に分岐し、石英砂層604に供給する被処理水を分散し、中心部に凹みが生じないようにする方法等も考えられるが、配管が複雑な形状を有すると、持ち運びの際に配管が破損する可能性が高く、仮に配管としてフレキシブルチューブを使用し配管破損を防止しようとしても、蓋体611のチューブ接続部(配管との接続部)の破損の可能性もあり、実用的とは言えない。  The lid 611 is provided with an inlet (not shown) for the water to be treated so as to project outward, and can be connected to the line L3 in a liquid-tight manner. The lid 611 is concave, and the inner bottom 616 is formed with a shallow groove 617 along the outer edge of the inner bottom, and is packed with a packing 618. When the sand filtration container 601 is closed, the opening of the sand filter 601 is opened. The sealing property is enhanced by bringing the end and the packing 618 into contact with each other. Immediately below the inlet of the inner bottom 616 of the lid body 611, the momentum of the water to be treated flowing from the line L3 is stopped, and a slight distance from the inner bottom 616 is provided in order to distribute and distribute the water to some extent on the filtration layer. A watering plate 612 is fixed at a position by two round bars 613. When the lid 611, the watering plate 612, and the round bar 613 are made of resin such as vinyl chloride, the lid 611, the watering plate 612, and the round bar 613 are fixed by welding or adhesion, for example. The watering plate 612 is a disk shape having a diameter that is about 2 to 10 times larger than the inner diameter of the pipe constituting the line L3, and is preferably about 1/3 to 1/5 of the inner diameter of the sand filtration container 601. Although the diameter of the water spray plate 612 is set to a size that can cover the inner area of the sand filtration container 601, it is also possible to provide a punching hole or the like in the water spray plate to spray water over the entire surface of the filtration layer of the sand filtration container 601. The installation situation at the site is unknown, and it is often difficult to install horizontally, and if the watering plate is tilted, the flow will be limited to one direction and will not be sprinkled all over. It is rather undesirable to make the watering plate 612 larger. On the other hand, when the watering plate 612 is not present or too small, the central portion of the quartz sand layer 604 is recessed by the momentum of the water to be treated flowing from the line L3, and an inverted conical hole is formed, so that a short circuit of water is likely to occur. . In a small portable sand filter cylinder 6, compactness and weight reduction are important points, so the filling volume and height cannot be increased. The filling height of the quartz sand (the height of the quartz sand layer 604) is preferably about 4 to 10 cm, but if a dent of about 2 to 3 cm in depth is generated at such a height, the possibility of short circuit is too large. . Therefore, it is desirable to install the watering plate 612 for portable use. A method of branching the pipes constituting L3 into a plurality of pipes before entering the sand filter cylinder 6 to disperse the water to be treated to be supplied to the quartz sand layer 604 so that no dents are generated in the central portion is also considered. However, if the piping has a complicated shape, there is a high possibility that the piping will be damaged during carrying. Even if a flexible tube is used as the piping to prevent the piping from being damaged, the tube connecting portion (piping) of the lid 611 There is a possibility of damage to the connection part), which is not practical.

空気取り入れバルブ607、水位調整バルブ609、及び配管608、610の口径はそれほど大きくなくてもよく、例えば内径8mm程度あればよい。空気取り入れバルブ607及び水位調整バルブ609は、自動バルブであっても手動バルブであってもよい。  The diameters of the air intake valve 607, the water level adjustment valve 609, and the pipes 608 and 610 do not have to be so large. For example, the inner diameter may be about 8 mm. The air intake valve 607 and the water level adjustment valve 609 may be automatic valves or manual valves.

空気層606は、手動ポンプ5の操作性にも影響している。すなわち、空気層606がない状態では、手動ポンプ5からL6に至るまでの簡易浄水装置100全体に亘って、一連に水で繋がった状態になり、手動ポンプ5の吐出時の抵抗が大きくなり、ポンプ操作員は過大な労力を要することになる。しかし、空気層606が存在すると、上述のように脈動を低減し得るのみならず、空気層606のクッション作用で手動ポンプ5の操作時にポンプ操作員に必要とされる力を軽減することが可能となる。また、手動ポンプ5の操作を停止しても、例えば停止時の砂ろ過筒6内の残圧が約50kPaあれば約15〜30秒間は飲料水が連続的に流れ続け、砂ろ過筒6内の残圧は最終的にゼロに至る。したがって、手動ポンプ5の操作中は、断続的に送水がなされても、砂ろ過筒6を通過後の水は、ほぼ脈動のない見事な均一流れになる。
その際、空気層606の容積当りの浄水量すなわち容積速度(空間速度)(SV)は、60〜120m/m/時程度であることが好ましい。
The air layer 606 also affects the operability of the manual pump 5. That is, in the state where there is no air layer 606, the entire state of the simple water purifier 100 from the manual pump 5 to L6 is connected with water in series, and the resistance at the time of discharge of the manual pump 5 increases. The pump operator is excessively labor intensive. However, the presence of the air layer 606 not only can reduce pulsation as described above, but also can reduce the force required for the pump operator when operating the manual pump 5 by the cushioning action of the air layer 606. It becomes. Further, even if the operation of the manual pump 5 is stopped, for example, if the residual pressure in the sand filtration cylinder 6 at the time of the stop is about 50 kPa, drinking water continuously flows for about 15 to 30 seconds. The residual pressure finally reaches zero. Therefore, during the operation of the manual pump 5, even if water is intermittently supplied, the water after passing through the sand filter cylinder 6 becomes a stunning uniform flow with almost no pulsation.
At that time, water purification dose or volume rate per volume of the air layer 606 (space velocity) (SV) is preferably 60~120m 3 / m 3 / about hour.

石英砂層604は、粒度が500〜850μm程度の天然の破砕物が好適に用いられる。粒度が大き過ぎると懸濁物質などの捕捉性能が落ち、小さ過ぎると石英砂層604の目詰まりが速く、短時間で大きな圧損を生じる傾向にある。このような粒度が500〜850μm程度の石英砂は、重量パーセントで石英砂層604全体の50%以上、好ましくは60〜90%程度含まれるとよい。また、人工的に丸い形状に整形された石英砂の充填高さをいくら高くしても懸濁物質の捕捉性能は上がり難い。これに対し、天然の破砕石英砂は、粉砕時に表面が荒れるため、表面に凹凸や角部が多く生じ、このような砂表面の角部や凸部の組み合わせで微細な懸濁粒子を捕捉することが可能となっていると考えられる。また、表面が角状で適度な粒径の石英砂であれば充填された石英砂層604では、石英砂層604のほぼ全域で種々の大きさの微小な懸濁物質を捕捉し得るので、従来のろ過装置で生じていたろ過上部表層に偏った目詰まりや微小懸濁物のリークがなく、長時間にわたり砂ろ過筒6を含め、後段の活性炭筒7や膜ろ過器8の浄化水量の低下や圧損上昇が起こらない。石英砂の充填高さ(石英砂層604の高さ)は、4〜10cm程度が好ましい。  The quartz sand layer 604 is preferably a natural crushed material having a particle size of about 500 to 850 μm. When the particle size is too large, the trapping performance of suspended substances and the like is lowered, and when it is too small, the quartz sand layer 604 is clogged quickly, and a large pressure loss tends to occur in a short time. Such quartz sand having a particle size of about 500 to 850 μm may be contained in a weight percentage of 50% or more, preferably about 60 to 90% of the entire quartz sand layer 604. In addition, the trapping performance of suspended solids hardly increases even if the filling height of the artificially shaped quartz sand is increased. On the other hand, natural crushed quartz sand has a rough surface during pulverization, so that there are many irregularities and corners on the surface, and fine suspended particles are captured by the combination of corners and protrusions on the sand surface. It is considered possible. In addition, if the surface is square and the silica sand has an appropriate particle size, the filled quartz sand layer 604 can capture fine suspended substances of various sizes almost over the entire area of the quartz sand layer 604. There is no uneven clogging or leakage of microsuspension in the upper surface layer of the filtration that has occurred in the filtration device, and the amount of purified water in the latter stage activated carbon cylinder 7 and membrane filter 8 including the sand filtration cylinder 6 over a long period of time No pressure loss rises. The filling height of quartz sand (the height of the quartz sand layer 604) is preferably about 4 to 10 cm.

リリース弁614は、砂ろ過筒6、活性炭筒7及び膜ろ過器8のいずれかが、目詰まりを起こし圧力が異常に上昇した場合の圧力緩和対策のため設けられたものである。また、手動ポンプ5の操作員が激しい往復操作をした場合には、浄水量が増し、砂ろ過筒6内の圧力が最大で150〜180kPa程度になるが、このような異常な圧力上昇を防ぐ対策としても有効である。また、手動ポンプ5の激しい操作でLVが10m/m/時程度を超えると、システム全体の浄化効率が下がるため、その未然防止策にもなる。リリース弁614の開放設定は、例えば100〜130kPaとするとよい。The release valve 614 is provided as a pressure relief measure when any of the sand filter cylinder 6, the activated carbon cylinder 7 and the membrane filter 8 is clogged and the pressure rises abnormally. In addition, when the operator of the manual pump 5 performs a reciprocal reciprocating operation, the amount of purified water is increased and the pressure in the sand filter cylinder 6 is about 150 to 180 kPa at the maximum, but such an abnormal pressure rise is prevented. It is also effective as a countermeasure. Further, if the LV exceeds about 10 m 3 / m 2 / hour due to intense operation of the manual pump 5, the purification efficiency of the entire system is lowered, which is a preventive measure. The release setting of the release valve 614 is preferably 100 to 130 kPa, for example.

上部不織布層605は、粗目フィルタ2で木の葉やビニール片等の粗大夾雑物が除去され、紙フィルタ4で0.05〜1mm程度の小粒子が捕捉されるため、懸濁粒子の捕捉というより、むしろ被処理水の分散と、簡易浄水装置100(携帯用浄水キット)を携帯して移動する際の石英砂層604の散逸防止が目的となる。上部不織布層605を構成する不織布の目付けは、100〜250g/m程度が良い。上部不織布605の厚みは厚いほど良いが、携行用なため、砂ろ過筒6をコンパクトにする制約があり、3〜5cm程度とすることが好ましい。なお、簡易浄水装置100(携帯用浄水キット)の販売時の形態としては、砂ろ過筒6内の充填物の形崩れ防止のため、上部不織布層605上の空気層606にダミーの段ボール材が入れられる。In the upper nonwoven fabric layer 605, coarse contaminants such as leaves and vinyl pieces are removed by the coarse filter 2, and small particles of about 0.05 to 1 mm are captured by the paper filter 4, so that rather than capturing suspended particles, Rather, the purpose is to disperse the water to be treated and to prevent the quartz sand layer 604 from being lost when the simple water purifier 100 (portable water purification kit) is carried and moved. The basis weight of the nonwoven fabric constituting the upper nonwoven fabric layer 605 is preferably about 100 to 250 g / m 2 . The thickness of the upper nonwoven fabric 605 is better as it is thicker. However, since the upper nonwoven fabric 605 is for carrying, there is a restriction to make the sand filter cylinder 6 compact, and it is preferable that the thickness is about 3 to 5 cm. In addition, as a form at the time of sale of the simple water purification apparatus 100 (portable water purification kit), a dummy cardboard material is used for the air layer 606 on the upper nonwoven fabric layer 605 in order to prevent the packing in the sand filter cylinder 6 from being deformed. Can be put.

下部不織布層603は、上層の石英砂が後工程に漏出するのを防止するための層で、下部不織布層603を構成する不織布の目付けは、上部不織布層605と同様に100〜250g/m程度が良い。また、下部不織布層603の充填前の厚みは3〜5cm程度が良いが、石英砂層604の充填時に石英砂層604の重量の影響で1.5〜2.5cm程度となる。The lower nonwoven fabric layer 603 is a layer for preventing the upper-layer quartz sand from leaking to the subsequent process, and the basis weight of the nonwoven fabric constituting the lower nonwoven fabric layer 603 is 100 to 250 g / m 2, similar to the upper nonwoven fabric layer 605. Good degree. Further, the thickness of the lower nonwoven fabric layer 603 before filling is preferably about 3 to 5 cm, but is about 1.5 to 2.5 cm due to the influence of the weight of the quartz sand layer 604 when the quartz sand layer 604 is filled.

砂ろ過容器601の側面下部の樹脂ペレット層602と連通する位置には、ろ過水出口(図示略)が突設して設けられており、ラインL4と液密に接続されており、上述のろ過層を通過したろ過水はろ過水出口を介してラインL4に排出される。  At a position communicating with the resin pellet layer 602 at the lower side of the side surface of the sand filtration container 601, a filtered water outlet (not shown) is provided so as to project from the line L4 in a liquid-tight manner. The filtered water that has passed through the bed is discharged to the line L4 through the filtered water outlet.

砂ろ過筒6、すなわち、石英砂層604の再生は、バケツ等の容器に移して浄水で洗浄することにより容易に再生することができる。
例えば、1日5時間運転して、5日間使用した未閉塞(まだ利用可能な状態)の石英砂層604をバケツに取って、本簡易浄水装置100で浄化した飲料水を3L加え、手回しで3回洗浄したところ、3回目の濁度は殆どなく透明に近くなった。1回の洗浄に要する時間は、僅か2〜3分程度で、このことは、石英砂の沈降性の良さと懸濁物質の剥離性の良さを示している。したがって、簡易浄水装置100の使用場所がどこであっても簡単に洗浄し、石英砂層604の再装填が可能である。また、石英砂層604の全域でろ過されていることを確認するために、石英砂層604を、上層部、中層部、下層部の3層に分けて分取し、水洗浄を実施したところ、3層とも多量の懸濁物質を包含しており、SS分析の結果からは有意な差がなく、一般的なろ過装置に共通している表層部での集中的な懸濁物質の捕捉がなく、石英砂層604全域での懸濁物質の捕捉がされたことが確認されている。
また、砂ろ過筒6と併行して行った各種のディスクフィルタ、砂ろ過、珪藻土ろ過、糸巻きフィルタ等の比較試験の結果から、砂ろ過筒6は懸濁物質の除去性、長時間のろ過差圧安定性、洗浄性、脈動防止等で明らかな優位性があることが判明している。
The sand filter cylinder 6, that is, the quartz sand layer 604, can be easily regenerated by transferring it to a bucket or the like and washing it with purified water.
For example, drive 5 hours a day, take 5 days of unblocked (still available) quartz sand layer 604 in a bucket, add 3 L of drinking water purified by this simple water purifier 100, and turn 3 After washing twice, there was almost no turbidity at the third time and it became almost transparent. The time required for one washing is only about 2 to 3 minutes, which indicates good sedimentation of quartz sand and good peelability of suspended substances. Therefore, it is possible to easily wash and reload the quartz sand layer 604 wherever the simple water purifier 100 is used. Further, in order to confirm that the entire area of the quartz sand layer 604 was filtered, the quartz sand layer 604 was separated into three layers of an upper layer portion, a middle layer portion, and a lower layer portion, and water washing was performed. Both layers contain a large amount of suspended solids, there is no significant difference from the results of SS analysis, there is no intensive suspended matter capture at the surface layer common to general filtration devices, It has been confirmed that suspended substances have been captured throughout the quartz sand layer 604.
In addition, from the results of comparative tests of various disk filters, sand filtration, diatomaceous earth filtration, thread-wound filters, etc., performed in parallel with the sand filter cylinder 6, the sand filter cylinder 6 is capable of removing suspended solids and filtering for a long time. It has been found that there is a clear advantage in pressure stability, detergency, pulsation prevention and the like.

図6は、本実施形態に用いられる往復動式手動ポンプ5の模式図である。図6に示すように、往復動式手動ポンプ5は、吸込口と吐出口が設けられ、上端が開口されたポンプケーシング(シリンダ)53と、ポンプケーシング53の開口端より挿入され、ポンプケーシング内に上下動自在に支持された軸部52とを備えている。吸込口と吐出口は、各々ラインL2及びラインL3に液密に接続される。軸部52の一端には、手持ち用の取っ手51が設けられており、取っ手51に繋がる軸部52を上下に往復させると、軸部52の他端側に設けられた図示せぬピストンがポンプケーシング53内を上下し、ポンプケーシング53内の容量を変動させる。これにより、ポンプケーシング53内にラインL2から水が吸込口を介して流入し、吐出口よりラインL3に水が排出される仕組みになっている。すなわち、操作員がポンプケーシング53の下端に設けられた踏み板54に足を乗せ、手動ポンプ5を固定し、取っ手51を上に持ち上げるとポンプケーシング53内に水を吸引し、取っ手51を下に押し込むとポンプケーシング53内に吸い込まれた水が排出される。  FIG. 6 is a schematic diagram of the reciprocating manual pump 5 used in the present embodiment. As shown in FIG. 6, the reciprocating manual pump 5 is provided with a suction casing and a discharge opening, and is inserted from a pump casing (cylinder) 53 having an upper end opened, and an opening end of the pump casing 53. And a shaft portion 52 supported so as to be movable up and down. The suction port and the discharge port are liquid-tightly connected to the line L2 and the line L3, respectively. A handle 51 for hand-held is provided at one end of the shaft portion 52. When the shaft portion 52 connected to the handle 51 is reciprocated up and down, a piston (not shown) provided on the other end side of the shaft portion 52 is pumped. The casing 53 is moved up and down to change the capacity of the pump casing 53. Thereby, the water flows into the pump casing 53 from the line L2 through the suction port, and the water is discharged from the discharge port to the line L3. That is, when an operator puts his / her foot on the tread plate 54 provided at the lower end of the pump casing 53 and fixes the manual pump 5 and lifts the handle 51 upward, water is sucked into the pump casing 53 and the handle 51 is lowered. When pushed in, the water sucked into the pump casing 53 is discharged.

このように、本実施形態に用いられるポンプ、砂ろ過筒、活性炭筒、膜ろ過器、粗目フィルタ、紙フィルタは、全て円筒状をしているため、配管を外し、各ユニットに解体することで、リュックサック等の携行用ケース内にも収容し易く、また、嵩張らないので持ち運びにも便利である。
以上、本発明について説明したが、本発明は上記実施形態及び後述の実施例に限定されて解釈されるものではなく、本発明の範囲を逸脱しない限り、当業者の知識に基づいて、種々の変更、修正、改良を加えることが可能である。
Thus, since the pump, sand filter cylinder, activated carbon cylinder, membrane filter, coarse filter, and paper filter used in this embodiment are all cylindrical, the pipes are removed and disassembled into each unit. It is easy to be accommodated in a carrying case such as a rucksack, and it is not bulky, so it is convenient to carry.
Although the present invention has been described above, the present invention is not construed as being limited to the above-described embodiments and examples described below. Various modifications can be made based on the knowledge of those skilled in the art without departing from the scope of the present invention. Changes, modifications and improvements can be made.

図1に示した簡易浄水装置100を組み立て、同図フローに従って試験を行った。なお、簡易浄水装置100の各構成要素の詳細については、下記のとおりである。
ラインL1〜L6を構成する配管には、耐水軟質ポリウレタンチューブを用いた。
粗目フィルタ2は、5mm径の複数の小孔を有する直径10cm、長さ17cmの略円筒形状の樹脂製の成形体を用い、水槽1内に浮かべた直径7cmの発泡スチロール製の球状フロート(浮子)3に吊り下げて設置した。
紙フィルタカートリッジを備えたろ過器4(以下、単に紙フィルタともいう)としては、図2乃至図4に示した構造を有するろ過器4(容器本体401および蓋体403の素材:塩化ビニール製、容器本体401の形状:直径8cm、長さ22の円筒状、袋状ろ紙402の展開時の寸法:18cm×40cm)を用いた。また、袋状ろ紙402は、パルプとPETが1対1の混繊維で、撥水処理をしておらず、加熱ロール処理を施した、厚さ60μm、目付け:30g/mのものを用いた。
砂ろ過筒6(以下、石英砂筒ともいう)は、図5に示した構造を有する砂ろ過筒6(本体601、蓋体611及び散水板612の素材:塩化ビニール製、本体601の外形:直径約13cm、全高約21cmの略円筒形状、散水板612の直径:40mm、空気取り入れバルブ607及び水位調整バルブ609:内径8mmの手動バルブ、配管608及び配管610の口径:内径8mm、石英砂層604の高さ:8cm、上部不織布層605の目付け及び下部不織布層603の目付:180g/m、上部不織布層605の厚さ:3cm、下部不織布層603の石英砂充填前の厚さ:3cm、樹脂ペレット層602の高さ:30mm、樹脂ペレット層602の材質等:直径10mmの樹脂ペレット)を用いた。
活性炭筒7及び膜ろ過器8は、両方とも、直径15cm、高さ35cmの略円筒形状の外形で、被処理水を筒体(活性炭筒7本体又は膜ろ過器8本体に相当)内に導入する被処理水入口と、ろ過処理後の水を外部に排出するろ過水出口とが筒体外周に突設されており、ポリウレタンチューブ(配管)と接続可能にされているものを用いた。活性炭筒7は、活性炭が充填されたカートッリジを装填するカートリッジ式で、活性炭カートリッジの活性炭充填率は4L(SV25m/m/h)のものを用いた。また、膜ろ過器8は、膜面積2.0m(線束1.2m/m/日)のUF膜を用いた。
ポンプ5は、特許文献1に記載の往復動式手動ポンプを用いた。
The simple water purifier 100 shown in FIG. 1 was assembled and tested according to the flow of FIG. In addition, about the detail of each component of the simple water purifier 100, it is as follows.
A water-resistant soft polyurethane tube was used for the pipes constituting the lines L1 to L6.
The coarse filter 2 uses a resin molded body of a substantially cylindrical shape having a diameter of 10 cm and a length of 17 cm having a plurality of small holes having a diameter of 5 mm, and a spherical float (float) made of polystyrene foam having a diameter of 7 cm floated in the water tank 1. 3 was hung and installed.
As the filter 4 having a paper filter cartridge (hereinafter also simply referred to as a paper filter), the filter 4 having the structure shown in FIGS. 2 to 4 (material of the container body 401 and the lid 403: made of vinyl chloride, The shape of the container main body 401: a diameter of 8 cm, a cylindrical shape having a length of 22, and a size when the bag-shaped filter paper 402 was developed: 18 cm × 40 cm was used. Further, the bag-like filter paper 402 is a fiber mixture of pulp and PET of 1: 1, which has not been subjected to water repellent treatment, has been subjected to heating roll treatment, and has a thickness of 60 μm and a basis weight of 30 g / m 2 . It was.
The sand filter cylinder 6 (hereinafter also referred to as a quartz sand cylinder) is a sand filter cylinder 6 having the structure shown in FIG. 5 (material of the main body 601, the lid body 611 and the watering plate 612: made of vinyl chloride, the outer shape of the main body 601: Approximately 13 cm in diameter, approximately 21 cm in height, approximately cylindrical shape, sprinkling plate 612 diameter: 40 mm, air intake valve 607 and water level adjustment valve 609: manual valve with an inner diameter of 8 mm, pipe 608 and pipe 610 caliber: inner diameter of 8 mm, quartz sand layer 604 Height: 8 cm, weight of upper nonwoven fabric layer 605 and weight of lower nonwoven fabric layer 603: 180 g / m 2 , thickness of upper nonwoven fabric layer 605: 3 cm, thickness of lower nonwoven fabric layer 603 before filling with quartz sand: 3 cm, The height of the resin pellet layer 602: 30 mm, the material of the resin pellet layer 602, etc .: resin pellets having a diameter of 10 mm) were used.
Both the activated carbon cylinder 7 and the membrane filter 8 have a substantially cylindrical shape with a diameter of 15 cm and a height of 35 cm, and the water to be treated is introduced into the cylinder (corresponding to the activated carbon cylinder 7 body or the membrane filter 8 body). The treated water inlet and the filtered water outlet for discharging the filtered water to the outside protruded from the outer periphery of the cylindrical body, and those that can be connected to the polyurethane tube (piping) were used. Activated carbon cylinder 7 is a cartridge type of loading Katorriji activated carbon is filled, the activated carbon packing ratio of the active carbon cartridge used was a 4L (SV25m 3 / m 3 / h). Also, membrane filtration unit 8, using a UF membrane having a membrane area 2.0 m 2 (flux 1.2m 3 / m 2 / day).
As the pump 5, a reciprocating manual pump described in Patent Document 1 was used.

浄水量(飲料水製造量)は、約60L/時で、紙フィルタ4の線束(LV)は10m/m/日、砂ろ過筒6の水面積当たりのLVは4.5m/m/時、砂ろ過筒6の容積速度(SV)は約45m/m/時とした。なお、砂ろ過筒6の空気層606のSVは90m/m/時とした。
水槽1内に貯留する被処理水(原水)として、珪藻土、水酸化マグネシウム等の各種懸濁物質と河川水を混合した擬似原水を用いた。
この擬似原水を用い、10時間連続運転した後の濁度除去結果及びその他の水質分析結果を表1に示す。
The amount of purified water (drinking water production amount) is about 60 L / hour, the bundle (LV) of the paper filter 4 is 10 m 3 / m 2 / day, and the LV per water area of the sand filter cylinder 6 is 4.5 m 3 / m. 2 / hour, the volume velocity (SV) of the sand filter cylinder 6 was about 45 m 3 / m 3 / hour. Incidentally, SV of the air layer 606 of sand filter tube 6 was 90m 3 / m 3 / h.
As the water to be treated (raw water) stored in the water tank 1, pseudo raw water in which various suspended substances such as diatomaceous earth and magnesium hydroxide were mixed with river water was used.
Table 1 shows the turbidity removal results and other water quality analysis results after 10 hours of continuous operation using this simulated raw water.

Figure 2010221206
Figure 2010221206

表1に示すように、原水で98度あった濁度を、砂ろ過筒6による処理後には1以下とすることができた。これにより、後段の活性炭筒7及び膜ろ過器8にかかる負荷を著しく低減することが可能となった。
また、表1に示すように、実施例の紙フィルタ4による処理後では、濁度除去率が約70%であった。これに対し、参考のため、上述した第一〜第五の条件を一つでも満たさない素材のフィルタを使用し、同様に実験を行ったところ、濁質除去能或いはろ過速度が劣る結果が得られた。すなわち、例えば、市販のコーヒーフィルタを使用した場合には、懸濁物質は殆ど通過してしまい、除去率は10%程度となり、極めて低かった。また、コーヒーの自動販売機で使用する業務用紙フィルタを使用した場合には、濁度は50〜60%程度除去されたものの、ろ過速度が遅くなった。したがって、第一〜第五の条件を満たす素材の袋状ろ紙402を使用することで、ろ過速度と濁質除去能のバランスに優れていることがわかった。
As shown in Table 1, the turbidity that was 98 degrees with the raw water could be reduced to 1 or less after the treatment with the sand filter cylinder 6. Thereby, it became possible to reduce significantly the load concerning the latter activated carbon cylinder 7 and the membrane filter 8. FIG.
Further, as shown in Table 1, the turbidity removal rate was about 70% after the treatment with the paper filter 4 of the example. On the other hand, for reference, when a filter made of a material that does not satisfy any of the first to fifth conditions described above was used and an experiment was conducted in the same manner, a result of inferior turbidity removal ability or filtration rate was obtained It was. That is, for example, when a commercially available coffee filter was used, the suspended substances almost passed, and the removal rate was about 10%, which was extremely low. Moreover, when the business paper filter used in the coffee vending machine was used, although the turbidity was removed by about 50 to 60%, the filtration rate became slow. Therefore, it turned out that it is excellent in the balance of filtration speed and turbidity removal ability by using the bag-shaped filter paper 402 of the raw material which satisfy | fills the 1st-5th conditions.

また、石英砂の粒度を変えて、上記と同様に行った比較試験の結果を表2に示した。表2に示すように、試験1では粒度100〜300μmのもの(粒径小)が64.9重量%含まれた石英砂を用いたが、1時間運転した後には石英砂の表層部に目詰まりが集中し、圧力損失(圧損)が85kPaまで上昇し、運転不能状態になった。また、試験3では粒径900〜1100μmのもの(粒径大)が74.9重量%含まれる石英砂を用いたが、濁度成分の捕捉性が悪く、紙フィルタ出口の濁度66度から僅か14%減の濁度57度であった。試験2では、粒度500〜850μmのもの(粒径中)を84.3重量%含む石英砂を用いたが、運転1時間後でも圧損は8kPaと運転開始直後の圧損と変わらず、また、濁度も1度未満とすることができ、ろ過能に優れていた。  In addition, Table 2 shows the results of a comparative test performed in the same manner as described above with the particle size of quartz sand changed. As shown in Table 2, in the test 1, quartz sand containing 64.9% by weight of particles having a particle size of 100 to 300 μm (small particle size) was used. Clogging concentrated, pressure loss (pressure loss) increased to 85 kPa, and operation became impossible. In Test 3, quartz sand containing 74.9% by weight of particles having a particle size of 900 to 1100 μm (large particle size) was used, but the trapping property of turbidity components was poor, and the turbidity from 66 ° at the paper filter outlet was low. The turbidity was only 14% decreased to 57 degrees. In Test 2, quartz sand containing 84.3% by weight of particles having a particle size of 500 to 850 μm (medium particle size) was used, but even after 1 hour of operation, the pressure loss was 8 kPa, which was the same as the pressure loss immediately after the start of operation. The degree could be less than 1 degree, and the filterability was excellent.

Figure 2010221206
Figure 2010221206

なお、現場試験として、東京都昭島市付近の多摩川で、図1の浄化フローに従い、5時間連続運転を行ったが、活性炭やUF膜の圧損上昇は全くなく、浄化水の水質は飲料水の水質基準(水道法第4条の規定に基づき、平成15年5月30日公布の「水質基準に関する省令」で規定する基準)として規定される、一般細菌、大腸菌を含む51項目をすべてクリアする結果であった。  In the field test, the Tamagawa River near Akishima City, Tokyo, was operated continuously for 5 hours according to the purification flow shown in Fig. 1. However, there was no increase in the pressure loss of the activated carbon or UF membrane, and the quality of the purified water was drinking water. Clear all 51 items including general bacteria and Escherichia coli stipulated as water quality standards (standards stipulated in “Ministerial Ordinance on Water Quality Standards” promulgated on May 30, 2003 based on Article 4 of the Water Supply Law) It was a result.

L1〜L6 配管
1 水槽
2 粗目フィルタ
3 フロート
4 ろ過器(紙フィルタ)
5 往復動式手動ポンプ
6 砂ろ過筒
7 活性炭筒
8 膜ろ過器
9 飲料水貯槽
100 簡易浄水装置
L1 to L6 Piping 1 Water tank 2 Coarse filter 3 Float 4 Filter (paper filter)
5 Reciprocating manual pump 6 Sand filter cylinder 7 Activated carbon cylinder 8 Membrane filter 9 Drinking water storage tank 100 Simple water purifier

Claims (12)

被処理水を汲み上げて送水するポンプと、
ろ過層として石英砂層を有する砂ろ過筒と、
活性炭を充填した活性炭筒及び/又は膜ろ過器と、
前記各構成要素を繋ぐ配管と、を有し、
前記膜ろ過器は、精密ろ過膜、限外ろ過膜又は逆浸透膜を備え、
前記ポンプ、前記砂ろ過筒、前記活性炭筒及び/又は膜ろ過器の順に、前記配管により各構成要素を連結し、ポンプで汲み上げられる被処理水を砂ろ過筒でろ過した後、活性炭筒及び/又は膜ろ過器に通水し、処理水を得る簡易浄水装置を組立可能なキットであって、
収容時には、各構成要素を分離した状態で携行用ケース内に収容し得ることを特徴とする携行型浄水キット。
A pump that pumps up and feeds the water to be treated;
A sand filter cylinder having a quartz sand layer as a filter layer;
An activated carbon cylinder and / or a membrane filter filled with activated carbon;
A pipe connecting the components,
The membrane filter comprises a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane,
The pump, the sand filter cylinder, the activated carbon cylinder and / or the membrane filter are connected in order to the constituent elements by the pipes, and the water to be pumped by the pump is filtered through the sand filter cylinder, and then the activated carbon cylinder and / or Or it is a kit that can assemble a simple water purification device that passes water through a membrane filter and obtains treated water,
A portable water purification kit characterized in that each component can be stored in a carrying case when housed.
前記石英砂層が、天然の母岩を破砕して得られる破砕石英砂からなり、500〜850μmの粒径のものを重量で全体の50%以上含むことを特徴とする請求項1に記載の携行型浄水キット。  The carrying according to claim 1, wherein the quartz sand layer is made of crushed quartz sand obtained by crushing natural host rock, and contains 50% or more of a particle having a particle diameter of 500 to 850 μm by weight. Type water purification kit. 前記砂ろ過筒によるろ過後のろ過水濁度が1度以下であることを特徴とする請求項1又は2に記載の携行型浄水キット。  The portable water purification kit according to claim 1 or 2, wherein the filtered water turbidity after filtration by the sand filter cylinder is 1 degree or less. 前記ポンプが往復動式手動ポンプなどの吐出脈動を生じるポンプであり、前記砂ろ過筒が、該砂ろ過筒内のろ過層の上方に前記ポンプにより送水される被処理水の脈動を低減するための空気層を備えていることを特徴とする請求項1乃至3の何れかに記載の携行型浄水キット。  The pump is a pump that generates discharge pulsation such as a reciprocating manual pump, and the sand filter cylinder reduces pulsation of water to be treated which is fed by the pump above the filtration layer in the sand filter cylinder. The portable water purification kit according to any one of claims 1 to 3, further comprising an air layer. 前記砂ろ過筒は、上部に被処理水を導入する導入口を、下部に処理水を取り出す取出し口を備え、前記ろ過層が、該ろ過層の上方に空気層が設けられるように形成されており、
該砂ろ過筒の上部にはさらに前記空気層と連通するように、ろ過筒内に空気を取り入れる空気取り入れ口と、ろ過筒内の圧力が一定圧力を超えた時にろ過筒内の空気を外部に放出するリリース弁とが設けられており、
前記ろ過層の最上部近傍の所定位置に、ろ過筒内の水位を調整するための水位調整バルブを備えた排出口が設けられており、
被処理水のろ過時においても、前記空気層が常時維持されるようにろ過筒内の水位と空気量を調節することを特徴とする請求項1乃至4の何れかに記載の携行型浄水キット。
The sand filter cylinder is provided with an inlet for introducing the water to be treated at the upper part and an outlet for taking out the treated water at the lower part, and the filtration layer is formed so that an air layer is provided above the filtration layer. And
An air intake port for taking air into the filter cylinder so as to further communicate with the air layer above the sand filter cylinder, and the air in the filter cylinder to the outside when the pressure in the filter cylinder exceeds a certain pressure And a release valve to release,
A discharge port equipped with a water level adjustment valve for adjusting the water level in the filtration cylinder is provided at a predetermined position near the top of the filtration layer,
The portable water purification kit according to any one of claims 1 to 4, wherein the water level and the amount of air in the filtration cylinder are adjusted so that the air layer is always maintained even during filtration of the water to be treated. .
前記砂ろ過筒は、前記導入口の下方に該導入口より流入する被処理水の勢いを止め、下方の前記ろ過層上に供給される被処理水を分散する散水板を備えることを特徴とする請求項1乃至5の何れかに記載の携行型浄水キット。  The sand filter cylinder includes a water spray plate that stops the momentum of the water to be treated flowing from the introduction port below the introduction port and disperses the treatment water supplied onto the filtration layer below. The portable water purification kit according to any one of claims 1 to 5. 前記携行型浄水キットが、さらに、前記砂ろ過筒の上流に配置される、使い捨て紙フィルタカートリッジを備えたろ過器を有することを特徴とする請求項1乃至6の何れかに記載の携行型浄水キット。  The portable water purification kit according to any one of claims 1 to 6, wherein the portable water purification kit further includes a filter provided with a disposable paper filter cartridge, which is disposed upstream of the sand filter cylinder. kit. 前記紙フィルタカートリッジを備えたろ過器が、
一端に底部を、他端に開口部を有し、前記底部又は底部近傍にろ過水を取り出す取出し口を有する筒型の容器本体と、
前記容器本体内に収容され、平面視略矩形状の扁平な袋状に形成され、一隅に小孔部を有する袋状ろ紙、及び一端が外方に突出するように該小孔部より該袋状ろ紙内に挿入され、該小孔部近傍で密着固定された接続管を有する紙フィルタカートリッジと、
前記紙フィルタカートリッジを前記容器本体に収容した際に前記容器本体内に流路となる間隙を形成するための多孔質体からなるシート状のスペーサと、
有底筒型で、肉厚の底部に貫通孔を有し、該貫通孔の外方側に内螺子部を有する、前記容器本体の開口部を閉塞する蓋体と、
前記内螺子部に螺合可能な外螺子部を一端に備える被処理水を導入する導入管と、
を備え、
前記ろ過器は、前記蓋体の貫通孔内の内螺子部に、前記導入管を螺合し、該貫通孔の他端側に、前記紙フィルタカートリッジの接続管を挿入することで前記導入管と該接続管を液密に接続し、前記紙フィルタカートリッジを、該紙フィルタカートリッジの袋状ろ紙部に重ね合わせた前記スペーサと共に前記接続管を軸として巻き取った状態で、前記容器本体内に収容し、前記蓋体で該容器本体の開口部を閉塞することで組立てられ、
前記導入管から前記接続管を介して前記袋状ろ紙内に被処理水を導入し、該袋状ろ紙を透過したろ過水を前記容器本体底部の取出し口より取り出し、被処理水より取り除いた汚濁物を前記袋状ろ紙内に溜めるようにしたことを特徴とする請求項7に記載の携行型浄水キット。
A filter equipped with the paper filter cartridge,
A cylindrical container body having a bottom at one end, an opening at the other end, and an outlet for taking out filtrated water at or near the bottom,
A bag-shaped filter paper housed in the container body and formed into a flat bag shape having a substantially rectangular shape in plan view and having a small hole portion at one corner, and the bag from the small hole portion so that one end protrudes outward. A paper filter cartridge having a connecting tube inserted into the filter paper and fixed in close contact with the small hole portion;
A sheet-like spacer made of a porous material for forming a gap serving as a flow path in the container body when the paper filter cartridge is accommodated in the container body;
A lid that closes the opening of the container body, having a bottomed cylindrical shape, having a through-hole in a thick bottom portion, and having an internal screw portion on the outer side of the through-hole;
An introduction pipe for introducing the water to be treated provided with an outer screw part that can be screwed into the inner screw part at one end;
With
The filter is configured such that the introduction pipe is screwed into an inner screw portion in the through hole of the lid body, and the connection pipe of the paper filter cartridge is inserted into the other end side of the through hole. And the connection tube in a liquid-tight manner, and the paper filter cartridge is wound around the connection tube together with the spacer superimposed on the bag-shaped filter paper portion of the paper filter cartridge in the container body. Housed and assembled by closing the opening of the container body with the lid,
Polluted water introduced from the introduction pipe into the bag-like filter paper through the connecting pipe, and filtered water that permeated through the bag-like filter paper was taken out from the outlet at the bottom of the container body and removed from the treated water. The portable water purification kit according to claim 7, wherein an object is stored in the bag-shaped filter paper.
前記袋状ろ紙が、パルプとPETの混繊維からなり、熱ローラによる加熱・加圧処理がされ、該処理後の厚みが50〜70μmであるろ紙を袋状に成形して製造されており、かつ、表面に撥水処理がされていないことを特徴とする請求項8に記載の携行型浄水キット。  The bag-shaped filter paper is made of a mixed fiber of pulp and PET, heated and pressurized by a heat roller, and manufactured after forming the filter paper having a thickness of 50 to 70 μm after the processing into a bag shape, The portable water purification kit according to claim 8, wherein the surface is not subjected to water repellent treatment. 前記接続管が樹脂管であり、前記袋状ろ紙と熱溶着により密着されていることを特徴とする請求項8又は請求項9に記載の携行型浄水キット。  The portable water purification kit according to claim 8 or 9, wherein the connection pipe is a resin pipe and is in close contact with the bag-like filter paper by heat welding. 前記携行型浄水キットが、さらに、木の葉、ビニール片等の粗大夾雑物を取り除くための粗目フィルタを有することを特徴とする請求項1乃至10の何れかに記載の携行型浄水キット。  The portable water purification kit according to any one of claims 1 to 10, wherein the portable water purification kit further includes a coarse filter for removing coarse impurities such as leaves and vinyl pieces. ろ過層として石英砂層を有し、該石英砂層が天然の母岩を破砕して得られる破砕石英砂からなり、500〜850μmの粒径のものを重量で全体の50%以上含むことを特徴とする砂ろ過筒。  It has a quartz sand layer as a filtration layer, the quartz sand layer is made of crushed quartz sand obtained by crushing natural host rock, and contains 50% or more of a particle having a particle size of 500 to 850 μm by weight. Sand filter cylinder.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102295369A (en) * 2011-08-16 2011-12-28 浦坚 Device and method for removing hardness in drinking water
JP2014073460A (en) * 2012-10-04 2014-04-24 Uerushii:Kk Portable water purification kit
CN104925975A (en) * 2015-05-19 2015-09-23 中国科学院寒区旱区环境与工程研究所 Water purification device for field science investigation
CN107399860A (en) * 2017-09-20 2017-11-28 王成帅 A kind of portable water purification kit
KR101817953B1 (en) * 2017-01-11 2018-01-12 케이원에코텍 주식회사 Eco-environment water production system
CN108862685A (en) * 2018-08-10 2018-11-23 安徽原野滤材有限公司 A kind of novel nano filter cloth
CN112850815A (en) * 2021-01-22 2021-05-28 深圳市金利源净水设备有限公司 Water treatment equipment capable of pumping clean water through pressure of raw water
WO2022016633A1 (en) * 2020-07-23 2022-01-27 山东海益化工科技有限公司 High-quality water treatment process specifically for chemical production
CN117466497A (en) * 2023-12-18 2024-01-30 青岛鑫源环保集团有限公司 Multi-level purifying treatment device for drinking water

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102295369A (en) * 2011-08-16 2011-12-28 浦坚 Device and method for removing hardness in drinking water
JP2014073460A (en) * 2012-10-04 2014-04-24 Uerushii:Kk Portable water purification kit
CN104925975A (en) * 2015-05-19 2015-09-23 中国科学院寒区旱区环境与工程研究所 Water purification device for field science investigation
CN104925975B (en) * 2015-05-19 2017-02-22 中国科学院寒区旱区环境与工程研究所 Water purification device for field science investigation
KR101817953B1 (en) * 2017-01-11 2018-01-12 케이원에코텍 주식회사 Eco-environment water production system
CN107399860A (en) * 2017-09-20 2017-11-28 王成帅 A kind of portable water purification kit
CN108862685A (en) * 2018-08-10 2018-11-23 安徽原野滤材有限公司 A kind of novel nano filter cloth
WO2022016633A1 (en) * 2020-07-23 2022-01-27 山东海益化工科技有限公司 High-quality water treatment process specifically for chemical production
CN112850815A (en) * 2021-01-22 2021-05-28 深圳市金利源净水设备有限公司 Water treatment equipment capable of pumping clean water through pressure of raw water
CN117466497A (en) * 2023-12-18 2024-01-30 青岛鑫源环保集团有限公司 Multi-level purifying treatment device for drinking water
CN117466497B (en) * 2023-12-18 2024-06-11 青岛鑫源环保集团有限公司 Multi-level purifying treatment device for drinking water

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