JP2011024849A - Washing machine - Google Patents

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JP2011024849A
JP2011024849A JP2009174951A JP2009174951A JP2011024849A JP 2011024849 A JP2011024849 A JP 2011024849A JP 2009174951 A JP2009174951 A JP 2009174951A JP 2009174951 A JP2009174951 A JP 2009174951A JP 2011024849 A JP2011024849 A JP 2011024849A
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water
voltage
ion
treatment device
washing tub
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Yasusuke Horiki
泰佑 堀木
Shigeru Sasabe
笹部  茂
Takemi Oketa
岳見 桶田
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Panasonic Corp
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Panasonic Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a washing machine provided with a water treatment apparatus which adsorbs components dissolved in water. <P>SOLUTION: The washing machine is provided with: the water treatment apparatus including ion exchangers which adsorb ion dissolved in water, an ion exchange membrane in which the ion exchangers having different polarities are arranged on the front and rear sides to dissociate the water and to remove the ion adsorbed to the ion exchangers, at least two electrodes which apply voltage to the ion exchange membrane, and a voltage control means which supplies voltage to the electrodes; a washing tub; a water supply means for supplying water to the washing tub; and a draining means which drains the washing tub. When the water treatment apparatus adsorbs, with the ion exchangers, the ion dissolved in the water to be supplied from the water supply means into the washing tub, voltage lower than the decomposition voltage of water is applied between the electrodes, so that the treated water from which the ion contained in the water is removed never contains electrolysis gas of water. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、水に溶解しているイオンを除去する水処理装置を備えた洗濯機に関するものである。   The present invention relates to a washing machine including a water treatment device that removes ions dissolved in water.

従来、この種の洗濯機は、図3に示すような構成であった(例えば、特許文献1参照)。以下、その構成、動作について説明する。   Conventionally, this type of washing machine has a configuration as shown in FIG. 3 (see, for example, Patent Document 1). The configuration and operation will be described below.

電解槽21中に電極22が隔膜23を介して対向して配置され、それぞれの電極22に電源24に接続され陽極、陰極を形成している。軟水化を行うさいは、電解槽21に、水を導入し、電源24により両電極間に電圧を印加する。水中に溶解しているカルシウムやマグネシウム等の陽イオンは、隔膜23を通過して陰極室へ移動する。洗濯は、水中に溶解していたカルシウムやマグネシウム等の陽イオンが減少した陽極室内の水を用いて行う。   Electrodes 22 are arranged in the electrolytic cell 21 so as to face each other with a diaphragm 23, and each electrode 22 is connected to a power source 24 to form an anode and a cathode. When softening the water, water is introduced into the electrolytic cell 21 and a voltage is applied between the electrodes by the power source 24. Cations such as calcium and magnesium dissolved in water pass through the diaphragm 23 and move to the cathode chamber. Washing is performed using water in the anode chamber in which cations such as calcium and magnesium dissolved in the water are reduced.

特許第3154765号公報Japanese Patent No. 3154765

しかしながら、前記従来の構成では、軟水化するさいに電気透析を行っており、水に電圧を印加しているが、印加電圧を適切に制御していないため処理水は水が電気分解して発生する水素ガスおよび酸素ガスを含む。処理水に溶け込んでいたガスは、やがて成長して気泡となり、処理水を導く流路の引き回しによっては流路やまた洗濯槽にガス溜まりができる可能性があった。   However, in the conventional configuration, electrodialysis is performed when softening water, and voltage is applied to water. However, since the applied voltage is not controlled appropriately, treated water is generated by electrolysis of water. Including hydrogen gas and oxygen gas. The gas dissolved in the treated water eventually grows into bubbles, and depending on the routing of the flow path for guiding the treated water, there is a possibility that gas can be accumulated in the flow path and also in the washing tub.

前記従来の課題を解決するために、本発明の洗濯機は、水に溶解しているイオンを吸着するイオン交換体と、表裏に極性の異なる前記イオン交換体を配置し水を解離して前記イオン交換体に吸着したイオンを脱離するイオン交換膜と、前記イオン交換膜に電圧を印加する少なくとも2つの電極と、前記電極に電圧を供給する電圧制御手段とを有する水処理装置と、洗濯槽と、前記洗濯槽に給水する給水手段と、前記洗濯槽の水を排水する排水手段とを有し、前記水処理装置が前記給水手段から前記洗濯槽に給水する水に溶解しているイオンを前記イオン交換体により吸着するさいは、前記電極間に水の分解電圧未満の電圧を印加するものである。   In order to solve the conventional problems, the washing machine according to the present invention includes an ion exchanger that adsorbs ions dissolved in water, and the ion exchangers having different polarities on the front and back sides to dissociate water and A water treatment apparatus comprising: an ion exchange membrane for desorbing ions adsorbed on the ion exchanger; at least two electrodes for applying a voltage to the ion exchange membrane; and a voltage control means for supplying a voltage to the electrodes; Ions that have a tub, water supply means for supplying water to the washing tub, and drainage means for draining water from the washing tub, and wherein the water treatment device is dissolved in the water supplied to the washing tub from the water supply means Is adsorbed by the ion exchanger, a voltage lower than the water decomposition voltage is applied between the electrodes.

これによって、水中のイオンが吸着され軟水となった処理水を得るさい、水が電気分解してガスを発生することがないので、処理水は水の電気分解ガスを含んでおらず、処理水を導く流路やまた洗濯槽にガスが溜まる可能性がない。   As a result, when obtaining treated water in which ions in the water are adsorbed and become soft water, the water does not electrolyze to generate gas, so the treated water does not contain water electrolysis gas. There is no possibility of gas accumulating in the flow path leading to the water or in the washing tub.

本発明の洗濯機は、水中のイオンを吸着し軟水となった処理水に水の電気分解ガスを含まないので、処理水の導く流路やまた洗濯槽にガスが溜まることが原理的になく、安全な製品を提供することができる。   The washing machine of the present invention does not contain water electrolysis gas in the treated water that has become soft water by adsorbing ions in the water, so there is no principle that gas accumulates in the flow path leading to the treated water or in the washing tub. Can provide safe products.

本発明の第1の実施の形態における洗濯機の構成図The block diagram of the washing machine in the 1st Embodiment of this invention 本発明の第1の実施の形態における水処理装置の構成図The block diagram of the water treatment apparatus in the 1st Embodiment of this invention 従来の給湯機の構成図Configuration of a conventional water heater

第1の発明は、洗濯機が、水に溶解しているイオンを吸着するイオン交換体と、表裏に極性の異なる前記イオン交換体を配置し水を解離して前記イオン交換体に吸着したイオンを脱離するイオン交換膜と、前記イオン交換膜に電圧を印加する少なくとも2つの電極と、前記電極に電圧を供給する電圧制御手段とを有する水処理装置と、洗濯槽と、前記洗濯槽に給水する給水手段と、前記洗濯槽の水を排水する排水手段とを有し、前記水処理装置が前記給水手段から前記洗濯槽に給水する水に溶解しているイオンを前記イオン交換体により吸着するさいは、前記電極間に水の分解電圧未満の電圧を印加することにより、水中のイオンが除去された処理水は水の電気分解ガスを含むことがなく、処理水を導く流路やまた洗濯槽にガスが溜まる可能性がない。   According to a first aspect of the present invention, an ion exchanger in which a washing machine adsorbs ions dissolved in water and an ion exchanger that dissociates water by disposing the ion exchangers having different polarities on the front and back and adsorbed on the ion exchanger An ion exchange membrane for desorbing water, at least two electrodes for applying a voltage to the ion exchange membrane, a water treatment device having voltage control means for supplying a voltage to the electrodes, a washing tub, and a washing tub Water supply means for supplying water and drainage means for draining water from the washing tub, and the water treatment device adsorbs ions dissolved in water supplied from the water supply means to the washing tub by the ion exchanger. In this case, by applying a voltage lower than the water decomposition voltage between the electrodes, the treated water from which ions in the water have been removed does not contain water electrolysis gas, and the flow path leading the treated water or Gas can accumulate in the washing tub There is no.

第2の発明は、洗濯機が、水に溶解しているイオンを吸着するイオン交換体と、表裏に極性の異なる前記イオン交換体を配置し水を解離して前記イオン交換体に吸着したイオンを脱離するイオン交換膜と、前記イオン交換膜に電圧を印加する少なくとも2つの電極と、前記電極間に電圧を供給する電圧制御手段とを有する水処理装置と、洗濯槽と、前記洗濯槽に給水する給水手段と、前記洗濯槽の水を排水する排水手段とを有し、前記水処理装置が前記イオン交換体に吸着したイオンを脱離するさいは、前記電極間に水解離電圧以上の電圧を印加することにより、水を解離してHイオンとOHイオンを生成し、水中のイオンを吸着したイオン交換体を再生することができる。 According to a second aspect of the present invention, an ion exchanger in which a washing machine adsorbs ions dissolved in water and an ion exchanger that dissociates water by disposing the ion exchangers having different polarities on the front and back and adsorbed on the ion exchanger Exchange membrane, at least two electrodes for applying a voltage to the ion exchange membrane, voltage control means for supplying voltage between the electrodes, a washing tub, and the washing tub Water supply means for supplying water and drainage means for draining the water in the washing tub, and when the water treatment device desorbs ions adsorbed to the ion exchanger, the water dissociation voltage is higher than the voltage between the electrodes. By applying this voltage, water can be dissociated to generate H + ions and OH ions, and an ion exchanger that adsorbs ions in water can be regenerated.

第3の発明は、特に、第2の発明の洗濯機の水処理装置が、イオン交換体に吸着したイオンを脱離するさいは、電極間に水の分解電圧未満の電圧を印加することにより、水中のイオンを吸着したイオン交換体を再生する再生水に水の電気分解ガスを含むことがなく、再生水を導く流路にガスが溜まる可能性がない。   In the third aspect of the invention, in particular, when the water treatment apparatus of the washing machine of the second aspect of the present invention desorbs ions adsorbed on the ion exchanger, a voltage lower than the water decomposition voltage is applied between the electrodes. The regenerated water that regenerates the ion exchanger that adsorbs ions in the water does not contain water electrolysis gas, and there is no possibility of gas collecting in the flow path that leads the regenerated water.

第4の発明は、特に、第2または3のいずれか1つの発明の洗濯機の水処理装置が、イオン交換体に吸着したイオンを脱離するさいは、前記水処理装置を経由した水が洗濯槽を経由せず、排水手段により機外へ排出することにより、排水に含まれる高濃度のイオンが洗濯槽等を通過せず迅速に排出されることから、洗濯機内に蓄積することがない。   In the fourth invention, in particular, when the water treatment device of the washing machine according to any one of the second or third invention desorbs ions adsorbed on the ion exchanger, water passing through the water treatment device By discharging to the outside of the machine by the drainage means without going through the washing tub, the high concentration ions contained in the drainage can be quickly discharged without passing through the washing tub etc., so that they do not accumulate in the washing machine. .

第5の発明は、特に、第1〜4のいずれか1つの発明の洗濯機が、水に含まれる不溶物を除去する粗ろ過手段を有し、水処理装置に流入する水を前記粗ろ過手段で処理することから、不溶物が水処理装置に堆積することがなく、水処理装置の長寿命化することができる。   In the fifth aspect of the invention, in particular, the washing machine according to any one of the first to fourth aspects of the invention has a coarse filtration means for removing insoluble matters contained in water, and the coarse filtration of water flowing into a water treatment device is performed. Since the treatment is performed by the means, insoluble matters are not deposited on the water treatment apparatus, and the life of the water treatment apparatus can be extended.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、本実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the present embodiment.

(実施の形態1)
図1は、本発明の第1の実施の形態における構成図である。
(Embodiment 1)
FIG. 1 is a configuration diagram according to the first embodiment of the present invention.

図1において、洗濯機は筐体1の内部に、洗濯槽2が回転自在に外槽3に収納されている。給水弁4に原水ラインが接続されており、原水ラインは、水道水、工業用水、地下水等の水源等から供給される。原水ラインの水は給水弁4、粗ろ過手段5を通り、水処理装置6に導かれる。水処理装置6により処理された水は、三方弁7により分岐され、一方は洗剤投入手段8を経由して洗濯槽2へ、一方は機外へ直接排出される。洗濯槽2の水は、
排水弁9により水処理装置6の排水流路と合流し機外に排出される。制御手段10は、筐体1内に収容されており、洗濯機の一連の動作および水処理装置6の制御を行う。
In FIG. 1, a washing machine has a washing tub 2 housed in a housing 1 and rotatably housed in an outer tub 3. A raw water line is connected to the water supply valve 4, and the raw water line is supplied from a water source such as tap water, industrial water, and groundwater. The water in the raw water line passes through the water supply valve 4 and the coarse filtration means 5 and is guided to the water treatment device 6. The water treated by the water treatment device 6 is branched by the three-way valve 7, one is directly discharged to the washing tub 2 via the detergent charging means 8, and the other is directly discharged outside the machine. The water in the washing tub 2 is
The drainage valve 9 joins the drainage flow path of the water treatment device 6 and is discharged out of the machine. The control means 10 is accommodated in the housing 1 and controls a series of operations of the washing machine and the water treatment device 6.

図2は、本発明の第1の実施の形態における水処理装置6の構成図である。水処理装置6について、さらに詳しく説明する。水処理装置6は、対向する1組の電極11a、11bと、水に溶解している陽イオンを吸着する陽イオン交換体12と水に溶解している陰イオンを吸着する陰イオン交換体13とが、表裏に極性が異なるよう張り合わせたイオン交換膜から構成している。イオン交換膜は、電極11間に複数枚積層しており、平板状の対向した電極11間に平面上にイオン交換膜を積層、また、半径の異なる同心円柱状の対向した電極11間に同心円状や螺旋状にイオン交換膜を積層してもよい。イオン交換体はスチレンまたはジビニルベンゼンの重合体または共重合体高分子を基本骨格とし、陽イオン交換体12はスルホン酸基またはアクリル酸やメタクリル酸等のカルボン酸基を導入しており、陰イオン交換体13は第4級アンモニウム基または第1〜3級アミノ基を導入している。イオン交換体をイオン交換膜に成膜するさい、イオン交換体をポリエチレンやポリプロピレン等の熱可塑性樹脂に混練分散させることで、膜の成形性が向上することができる。表裏に極性が異なるようイオン交換体を張り合わせたイオン交換膜は、バイポーラ膜と呼ばれ、電圧を印加することでイオン交換体の界面で水の解離が促進されるので、低電圧で水の解離を行うことができる。   FIG. 2 is a configuration diagram of the water treatment device 6 according to the first embodiment of the present invention. The water treatment device 6 will be described in more detail. The water treatment device 6 includes a pair of opposing electrodes 11a and 11b, a cation exchanger 12 that adsorbs cations dissolved in water, and an anion exchanger 13 that adsorbs anions dissolved in water. Are composed of ion-exchange membranes that are bonded so that the polarities are different on the front and back sides. A plurality of ion exchange membranes are laminated between the electrodes 11, an ion exchange membrane is laminated on a flat surface between the flat electrodes 11, and concentric circles are formed between the concentric cylindrical electrodes 11 having different radii. Alternatively, an ion exchange membrane may be laminated spirally. The ion exchanger is based on a polymer or copolymer polymer of styrene or divinylbenzene, and the cation exchanger 12 is introduced with a sulfonic acid group or a carboxylic acid group such as acrylic acid or methacrylic acid. The body 13 has introduced a quaternary ammonium group or a primary to tertiary amino group. When forming the ion exchanger on the ion exchange membrane, the formability of the membrane can be improved by kneading and dispersing the ion exchanger in a thermoplastic resin such as polyethylene or polypropylene. Ion exchange membranes that have ion exchangers with different polarities on the front and back are called bipolar membranes. Dissociation of water at low voltage is promoted by applying a voltage to promote water dissociation at the interface of the ion exchanger. It can be performed.

以上のように構成した洗濯機について、以下その動作、作用を説明する。   About the washing machine comprised as mentioned above, the operation | movement and an effect | action are demonstrated below.

洗濯機は、マイクロコンピューターを搭載した制御手段10により、給水弁4、三方弁7、排水弁9、洗濯槽2の回転を自動制御して洗濯工程およびすすぎ工程を行う。   The washing machine performs the washing process and the rinsing process by automatically controlling the rotation of the water supply valve 4, the three-way valve 7, the drain valve 9, and the washing tub 2 by the control means 10 equipped with a microcomputer.

水処理装置6は、水中に溶解しているイオンをイオン交換体で吸着するさいと、イオン交換体に吸着したイオンを脱離するさいとで、動作が異なるので、まず、水処理装置6が水中のイオンをイオン交換体で吸着するさいについて説明する。   The operation of the water treatment device 6 differs depending on whether the ions dissolved in the water are adsorbed by the ion exchanger or the ions adsorbed on the ion exchanger are desorbed. A description will be given of adsorption of ions in water with an ion exchanger.

水処理装置6が水中に溶解しているイオンを吸着するさいは、給水弁4を開放し、原水ラインの水が水処理装置6に流入する。水処理装置6により水中に溶解しているイオンが除去された浄水は洗剤投入手段8を経由して洗濯槽2に導かれる。また、一部の浄水は直接洗濯槽2に導かれる。所定時間、洗浄工程を行った後、排水弁9を開放して洗濯槽2の洗浄水を排水する。続いて、同様にして再度給水し、すすぎ工程を行う。   When the water treatment device 6 adsorbs ions dissolved in water, the water supply valve 4 is opened, and the water in the raw water line flows into the water treatment device 6. The purified water from which ions dissolved in water are removed by the water treatment device 6 is guided to the washing tub 2 via the detergent charging means 8. A part of the purified water is directly led to the washing tub 2. After performing a washing process for a predetermined time, the drain valve 9 is opened to drain the washing water in the washing tub 2. Subsequently, water is again supplied in the same manner, and a rinsing process is performed.

ここで、水処理装置6の動作について詳しく説明する。水処理装置6では、水中に溶解した陽イオンCa、Mg、Na、Mn、Fe等の各イオンは陽イオン交換体12で水素イオンに、水中に溶解した陰イオンCl、炭酸、硫酸、硝酸等の各イオンは陰イオン交換体13で水酸化物イオンにイオン交換することで、水中に溶解している各種イオンをイオン交換体に吸着する。イオン交換体がイオンを吸着するさい、イオン交換膜の陽イオン交換体12側の電極11aを陽極、陰イオン交換体13側の電極11bを陰極となるよう電圧を印加することで、水処理装置6内のイオンがイオン交換体に移動するので、イオン交換体のイオン吸着速度を増加させることができる。そのさい、水分子が電気分解し水素分子と酸素分子を生成する水の理論分解電圧は1.226Vであるので、水の分解電圧未満の電圧を印加することで、水素ガスおよび酸素ガスが発生することなく水に溶解しているイオンをイオン交換体で効率的に吸着することができる。水処理装置6で水に溶解しているイオンを吸着することで、衣類を洗浄するさい洗剤の効果を高めることができ、洗浄力の向上、洗浄時間の短縮、省エネが可能となる。また、洗剤投入手段8や洗濯槽2に金属石鹸が生成することがないので、洗剤投入手段8や洗濯槽2を清浄に保つことができる。また、陰イオンによる腐食の促進等を防止することができる。また、pHの偏った水を処理した場合は、酸性の場合はアニオン種を水酸化物イオンに、塩基性の場合はカチオン種を
水素イオンに交換することで中性の水に近づけることができるので、水処理装置6により処理した水は、pHによる腐食を防止することができる。また、水の分解電圧未満の電圧を印加していることで、処理水は水の分解ガスを含有しておらず、洗濯槽2や排水経路に水の分解ガスが蓄積することがない。
Here, the operation of the water treatment device 6 will be described in detail. In the water treatment device 6, ions such as cations Ca, Mg, Na, Mn, Fe dissolved in water are converted into hydrogen ions by the cation exchanger 12, and anions Cl, carbonic acid, sulfuric acid, nitric acid, etc. dissolved in water. These ions are ion-exchanged to hydroxide ions by the anion exchanger 13 to adsorb various ions dissolved in water to the ion exchanger. When the ion exchanger adsorbs ions, a voltage is applied so that the electrode 11a on the cation exchanger 12 side of the ion exchange membrane serves as an anode, and the electrode 11b on the anion exchanger 13 side serves as a cathode. Since the ions in 6 move to the ion exchanger, the ion adsorption rate of the ion exchanger can be increased. At that time, since the theoretical decomposition voltage of water in which water molecules are electrolyzed to generate hydrogen molecules and oxygen molecules is 1.226 V, hydrogen gas and oxygen gas are generated by applying a voltage lower than the water decomposition voltage. Ions that are dissolved in water can be efficiently adsorbed by the ion exchanger without being carried out. By adsorbing ions dissolved in water with the water treatment device 6, it is possible to enhance the effect of the detergent for washing the clothes, thereby improving the cleaning power, shortening the cleaning time, and saving energy. Moreover, since no metal soap is generated in the detergent charging means 8 and the washing tub 2, the detergent charging means 8 and the washing tub 2 can be kept clean. In addition, promotion of corrosion due to anions can be prevented. Also, when water with a non-uniform pH is treated, it can be brought close to neutral water by exchanging the anion species with hydroxide ions when acidic and the cation species with hydrogen ions when basic. Therefore, the water treated by the water treatment device 6 can prevent corrosion due to pH. In addition, by applying a voltage lower than the water decomposition voltage, the treated water does not contain water decomposition gas, and water decomposition gas does not accumulate in the washing tub 2 or the drainage path.

なお、水処理装置6で水に溶解しているイオンを吸着するさいに、電極11間に電圧を印加しなくてもよい。イオン交換体が水に溶解しているイオンを吸着する作用に変わりはなく、処理水に水の分解ガスを含有しない効果も変わらない。   Note that when the water treatment device 6 adsorbs ions dissolved in water, it is not necessary to apply a voltage between the electrodes 11. The effect of the ion exchanger adsorbing ions dissolved in water remains the same, and the effect of not containing the decomposition gas of water in the treated water remains the same.

次に、水処理装置6がイオン交換体に吸着したイオンを脱離するさいの動作、作用を説明する。   Next, the operation and action when the water treatment device 6 desorbs ions adsorbed on the ion exchanger will be described.

イオン交換体がイオンを脱離するさいは、原水ラインより給水弁4に導かれた水は、水処理装置6で処理された後、三方弁7で切換えられ筐体1より排出される。水処理装置6では、イオン交換膜の陽イオン交換体12側の電極11aを陰極、陰イオン交換体13側の電極11bを陽極となるよう電圧を印加する。水分子が水素イオンと水酸化物イオンに解離する水の理論解離電圧は0.828Vであるので、水の解離電圧以上の電圧を印加することでイオン交換膜の陽イオン交換体12と陰イオン交換体13の界面で水が解離し、イオン交換体に吸着したイオンと交換し脱離することでイオン交換体が再生する。印加電圧を水の分解電圧未満にすることで、処理水は水の分解ガスを含有しないので、洗濯機から排出する間の排水経路で水の分解ガスが成長して気泡となり溜まることを防止することができる。   When the ion exchanger desorbs ions, the water guided from the raw water line to the water supply valve 4 is treated by the water treatment device 6 and then switched by the three-way valve 7 and discharged from the housing 1. In the water treatment device 6, a voltage is applied so that the electrode 11a on the cation exchanger 12 side of the ion exchange membrane serves as a cathode and the electrode 11b on the anion exchanger 13 side serves as an anode. Since the theoretical dissociation voltage of water at which water molecules dissociate into hydrogen ions and hydroxide ions is 0.828 V, the cation exchanger 12 and the anion of the ion exchange membrane can be applied by applying a voltage higher than the water dissociation voltage. Water is dissociated at the interface of the exchanger 13, and exchanged with ions adsorbed on the ion exchanger and desorbed to regenerate the ion exchanger. By making the applied voltage less than the decomposition voltage of water, the treated water does not contain the decomposition gas of water, so it prevents the decomposition gas of water from growing and collecting in the drainage path while discharging from the washing machine. be able to.

なお、排水流路の配管径を細くし排水流路を流れる排水の流速を十分に増加し排水流路内に気泡が滞留しないようにすることで、水の分解ガスが溜まることを防止することができる。水の分解ガスを確実に給湯機から排出できることから、水を解離しイオン交換体を再生するのに十分な電流、電圧を与えることができ、再生効率を向上することができるので、再生時間を短縮、再生排水を低減することができる。   In addition, by reducing the pipe diameter of the drainage channel and increasing the flow rate of the drainage flowing through the drainage channel sufficiently so that bubbles do not stay in the drainage channel, it is possible to prevent water decomposition gas from accumulating. Can do. Since the water decomposition gas can be reliably discharged from the water heater, sufficient current and voltage can be applied to dissociate the water and regenerate the ion exchanger, and the regeneration efficiency can be improved. Shortening and regeneration wastewater can be reduced.

粗ろ過手段5について説明する。水処理装置6は、水に溶解しているイオンをイオン交換体で確実に吸着するため、イオン交換膜が近接した状態で積層することが望ましが、イオン交換膜の間が僅少であるため、不溶物が堆積する可能性がある。粗ろ過手段5の除去性能は、イオン交換膜の間隔と同様またはより細かな不溶物を除去することができるようにする必要がある。粗ろ過手段5は、糸巻きフィルタ、プリーツフィルタ、中空糸フィルタ等の精密ろ過(MF)により形成し、原水に含まれる砂や鉄さび等の不溶性物質をろ過除去する。配置場所は、粗ろ過手段5に原水ラインの水圧がかからない給水弁4の下流側に設置することが望ましい。なお、原水ラインの水に不溶物が多く存在し、給水弁4の開放/閉塞の動作に問題が起こるような場合は、給水弁4の上流側に設置してもよい。また、粗ろ過手段は水処理手段6に流入する水を処理することから、洗浄槽2へ導かれる水も粗ろ過手段5で処理することができるので、洗浄槽2を清浄に保つことができ、また、衣類を不溶物の汚染から防ぐことができる。   The rough filtration means 5 will be described. The water treatment device 6 desirably adsorbs ions dissolved in water with an ion exchanger, so that the ion exchange membranes are desirably stacked in close proximity, but there is little space between the ion exchange membranes. Insoluble materials may accumulate. The removal performance of the coarse filtration means 5 needs to be able to remove insoluble matters that are similar to or finer than the interval of the ion exchange membrane. The coarse filtration means 5 is formed by microfiltration (MF) such as a thread wound filter, a pleated filter, and a hollow fiber filter, and removes insoluble substances such as sand and iron rust contained in the raw water by filtration. It is desirable that the arrangement location be installed on the downstream side of the water supply valve 4 where the rough filtration means 5 is not subjected to the water pressure of the raw water line. In addition, when there are many insolubles in the water of the raw water line and a problem occurs in the operation of opening / closing the water supply valve 4, it may be installed upstream of the water supply valve 4. Moreover, since the coarse filtration means treats the water flowing into the water treatment means 6, the water guided to the washing tank 2 can also be treated by the coarse filtration means 5, so that the washing tank 2 can be kept clean. In addition, clothing can be prevented from contamination with insoluble materials.

なお、水処理装置6により処理された水を分岐するさい三方弁7を用いているが、流路の切換えは三方弁に限定されることはなく、流路の開閉を行う二方の電磁弁等を複数組み合わせても、流路の切換えを行うことができれば構わない。   Although the three-way valve 7 is used to branch the water treated by the water treatment device 6, the switching of the flow path is not limited to the three-way valve, and the two-way electromagnetic valve that opens and closes the flow path Even if a plurality of combinations are combined, the flow path can be switched.

このように本発明の給湯機は、水に溶解しているイオンをイオン交換体で吸着、また、電圧を印加することで水を解離させ吸着したイオンを脱離しイオン交換体を再生することができる。交互に吸着脱離運転を行うことで、使用者はメンテナンスすることなく連続的にイオンを除去した処理水を利用することができ、また、得られる処理水は水の分解ガス
を含まないことから安全である。洗濯機の洗浄性能の向上、洗浄時間の短縮、省エネと共に機器の信頼性および寿命を向上することができ、さらに高硬度地域や井戸水等の過酷な原水に対しても適応することができる。
As described above, the water heater of the present invention can adsorb ions dissolved in water with an ion exchanger, and can dissociate water by applying a voltage to desorb the adsorbed ions to regenerate the ion exchanger. it can. By performing adsorption and desorption operation alternately, the user can use the treated water from which ions have been continuously removed without maintenance, and the obtained treated water does not contain water decomposition gas. It is safe. The washing performance of the washing machine can be improved, the washing time can be shortened, energy can be saved, and the reliability and life of the equipment can be improved.

以上のように、本発明にかかる水処理装置を備えた洗濯機は、原水の溶解イオンを吸着除去することができ、また得られた処理水は水の分解ガスを含まないことから、家庭用、産業用に制限されることなく、安全な処理水を利用する洗浄システムに適応することができる。   As described above, the washing machine provided with the water treatment apparatus according to the present invention can adsorb and remove dissolved ions of raw water, and the treated water obtained does not contain water decomposition gas. Without being restricted to industrial use, it can be applied to a cleaning system that uses safe treated water.

2 洗濯槽
4 給水手段
6 水処理装置
9 排水手段
10 制御手段
2 Washing tank 4 Water supply means 6 Water treatment device 9 Drainage means 10 Control means

Claims (5)

水に溶解しているイオンを吸着するイオン交換体と、表裏に極性の異なる前記イオン交換体を配置し水を解離して前記イオン交換体に吸着したイオンを脱離するイオン交換膜と、前記イオン交換膜に電圧を印加する少なくとも2つの電極と、前記電極に電圧を供給する電圧制御手段とを有する水処理装置と、洗濯槽と、前記洗濯槽に給水する給水手段と、前記洗濯槽の水を排水する排水手段とを有し、前記水処理装置が前記給水手段から前記洗濯槽に給水する水に溶解しているイオンを前記イオン交換体により吸着する際は、前記電極間に水の分解電圧未満の電圧を印加する洗濯機。 An ion exchanger that adsorbs ions dissolved in water, an ion exchange membrane that disposes the ions adsorbed on the ion exchanger by dissociating water by disposing the ion exchangers having different polarities on the front and back, A water treatment device having at least two electrodes for applying a voltage to the ion exchange membrane; a voltage control means for supplying a voltage to the electrodes; a washing tub; a water supply means for supplying water to the washing tub; Drainage means for draining water, and when the water treatment device adsorbs ions dissolved in water supplied from the water supply means to the washing tub with the ion exchanger, A washing machine that applies a voltage lower than the decomposition voltage. 水に溶解しているイオンを吸着するイオン交換体と、表裏に極性の異なる前記イオン交換体を配置し水を解離して前記イオン交換体に吸着したイオンを脱離するイオン交換膜と、前記イオン交換膜に電圧を印加する少なくとも2つの電極と、前記電極間に電圧を供給する電圧制御手段とを有する水処理装置と、洗濯槽と、前記洗濯槽に給水する給水手段と、前記洗濯槽の水を排水する排水手段とを有し、前記水処理装置が前記イオン交換体に吸着したイオンを脱離する際は、前記電極間に水解離電圧以上の電圧を印加する洗濯機。 An ion exchanger that adsorbs ions dissolved in water, an ion exchange membrane that disposes the ions adsorbed on the ion exchanger by dissociating water by disposing the ion exchangers having different polarities on the front and back, A water treatment device having at least two electrodes for applying a voltage to the ion exchange membrane, and a voltage control means for supplying a voltage between the electrodes, a washing tub, a water supply means for supplying water to the washing tub, and the washing tub A washing machine that applies a voltage higher than a water dissociation voltage between the electrodes when the water treatment device desorbs ions adsorbed to the ion exchanger. 水処理装置がイオン交換体に吸着したイオンを脱離する際は、電極間に水の分解電圧未満の電圧を印加する請求項2に記載の洗濯機。 The washing machine according to claim 2, wherein when the water treatment device desorbs ions adsorbed on the ion exchanger, a voltage lower than the water decomposition voltage is applied between the electrodes. 水処理装置がイオン交換体に吸着したイオンを脱離するさいは、前記水処理装置を経由した水が洗濯槽を経由せず、排水手段により機外へ排出する請求項2または3に記載の洗濯機。 The water treatment device according to claim 2 or 3, wherein when the water treatment device desorbs the ions adsorbed on the ion exchanger, the water passing through the water treatment device is discharged out of the machine by the drainage means without going through the washing tub. Washing machine. 水に含まれる不溶物を除去する粗ろ過手段を有し、水処理装置に流入する水を前記粗ろ過手段で処理する請求項1〜4いずれか1項に記載の洗濯機。
The washing machine according to any one of claims 1 to 4, further comprising a coarse filtration unit that removes insoluble matters contained in water, wherein water flowing into a water treatment device is treated by the coarse filtration unit.
JP2009174951A 2009-07-28 2009-07-28 Washing machine Pending JP2011024849A (en)

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