JP2014068798A - Washing machine, and washing method - Google Patents

Washing machine, and washing method Download PDF

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JP2014068798A
JP2014068798A JP2012216885A JP2012216885A JP2014068798A JP 2014068798 A JP2014068798 A JP 2014068798A JP 2012216885 A JP2012216885 A JP 2012216885A JP 2012216885 A JP2012216885 A JP 2012216885A JP 2014068798 A JP2014068798 A JP 2014068798A
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water
washing tub
washing
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water supply
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Koji Yamanaka
弘次 山中
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Organo Corp
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Japan Organo Co Ltd
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PROBLEM TO BE SOLVED: To provide a washing machine and a washing method capable of reducing a usage amount of detergent and saving washing costs while maintaining a washing effect without requiring special additional equipment in the washing of fiber and a fiber product.SOLUTION: A washing machine 1 includes: a water supply pipe 4 in a sealable washing tub 2; a water supply valve 8; a water supply pressure adjustment valve 7; an exhaust pipe 6; an exhaust valve 10; and a control device for controlling these. The control device introduces tap water into the washing tub 2 by supply pressure of water supply by opening the water supply valve 8 in a state where the washing tub 2 is sealed, and also, it allows air in the washing tub 2 to dissolve in the water in the washing tub 2 in such a manner that total dissolved gas concentration in water becomes 120% or more of saturation solubility under atmospheric pressure by controlling the water supply pressure adjustment valve 7 and the exhaust valve 10.

Description

本発明は、家庭用または業務用の洗濯機に関し、より具体的には洗濯効果を維持しながら洗剤使用量を低減する洗濯機および洗濯方法に関する。   The present invention relates to a household or commercial washing machine, and more specifically to a washing machine and a washing method for reducing the amount of detergent used while maintaining a washing effect.

繊維、繊維製品などの洗濯において、洗浄力の向上、洗濯時間の短縮、洗濯コストの節減、生地の傷みの抑制は求めて止まない目標であり、これを実現するために、洗剤、助剤、洗濯機などの開発が続けられてきた。   In the washing of textiles and textile products, improvement of detergency, reduction of washing time, reduction of washing costs, and suppression of fabric damage are continual goals. To achieve this, detergents, auxiliaries, Development of washing machines has been continued.

一方、家庭用、業務用に係わらず、洗濯に使用する水、例えば洗濯用水やすすぎ用水としては、水道水、井戸水、湖沼水、河川水などをそのまま用いるか、これらに濾過、殺菌などの処理を行って用いていた。つまり、これらの水に溶解している溶存気体、例えば溶存酸素や溶存窒素などの濃度については放置され、長年にわたってコントロールされることはほとんどなかった。したがって洗濯やすすぎは、下記の例外を除いては通常空気飽和の水により行われていた。   On the other hand, regardless of household use or business use, as water used for washing, for example, washing water and rinsing water, tap water, well water, lake water, river water, etc. are used as they are, or they are treated by filtration, sterilization, etc. I used it. In other words, the concentration of dissolved gas dissolved in water, such as dissolved oxygen and dissolved nitrogen, was left uncontrolled and was hardly controlled for many years. Therefore, washing and rinsing were usually performed with air-saturated water with the following exceptions.

これに対して、洗濯用水の溶存ガスをコントロールする試みとして、特許文献1には、洗濯物を密閉した洗濯槽内に入れ、この洗濯槽内を減圧方向に圧力変化させて、洗濯用水に溶解している気体を気泡化させて洗濯物に作用させる方法が開示されている。さらに、前記洗濯槽内を減圧方向に圧力変化させる為に、洗濯槽内を一旦加圧した後、常圧または負圧にすることが開示されている。   On the other hand, as an attempt to control the dissolved gas of washing water, Patent Document 1 discloses that the laundry is put in a sealed washing tub, and the pressure in the washing tub is changed in the decompression direction to dissolve in the washing water. A method is disclosed in which a gas that is flowing is bubbled to act on laundry. Furthermore, in order to change the pressure in the washing tub in the pressure-reducing direction, it is disclosed that the inside of the washing tub is once pressurized and then brought to normal pressure or negative pressure.

また特許文献2において、圧力容器内に水道水とガスボンベ内のCO2ガスを導入することでCO2溶解水を生成し、このCO2溶解水を洗濯槽内の水に供給する方法が開示されている。この方法では、前記CO2溶解水が洗濯槽内の水に供給されると、洗濯槽内の水にCO2ガスの微細気泡が発生し、その微細気泡によって洗濯物の汚れを落とす効果が生じる。 Patent Document 2 discloses a method of generating CO 2 dissolved water by introducing tap water and CO 2 gas in a gas cylinder into a pressure vessel, and supplying this CO 2 dissolved water to the water in the washing tub. ing. In this method, when the CO 2 -dissolved water is supplied to the water in the washing tub, fine bubbles of CO 2 gas are generated in the water in the washing tub, and the effect of removing dirt from the laundry is generated by the fine bubbles. .

特開平5-309195号公報JP-A-5-309195 特開2001-87587号公報Japanese Patent Laid-Open No. 2001-87587

洗濯に於いて洗浄力を増すには、洗剤濃度を増すこと、水温を上げること、pHを上げること、水流剪断速度を上げることなども可能であるが、これらの方法は洗浄コストの増加、廃水汚染の増加、衣類の縮みの発生、生地の傷みの増加などを招き好ましくない。   In order to increase the washing power in washing, it is possible to increase the detergent concentration, raise the water temperature, raise the pH, raise the water shear rate, etc., but these methods increase the washing cost, waste water This is undesirable because it increases contamination, shrinkage of clothing, and increases in fabric damage.

また、特許文献1及び2に開示されるような方法では、洗濯用水にガスを溶解させる設備や、洗濯槽内の水からガスの気泡を発生させる設備などが必要である。すなわち特許文献1に開示の洗濯機では、密閉された洗濯槽内を加圧/減圧するポンプが用意されており、特許文献2に開示の洗濯機では、洗濯槽内の水に供給するCO2溶解水を生成するために圧力容器やCO2ガスボンベが用意されている。このようにガス溶解に関する付帯設備が必要なため、洗濯機が高価になるという課題がある。 Further, the methods disclosed in Patent Documents 1 and 2 require equipment for dissolving gas in washing water, equipment for generating gas bubbles from water in the washing tub, and the like. That is, the washing machine disclosed in Patent Document 1 is provided with a pump for pressurizing / depressurizing the inside of a closed washing tub. In the washing machine disclosed in Patent Document 2, CO 2 supplied to the water in the washing tub is prepared. A pressure vessel and a CO 2 gas cylinder are prepared to generate dissolved water. Thus, since the incidental installation regarding gas dissolution is required, there exists a subject that a washing machine becomes expensive.

本発明の目的はこれらの問題や、さらには手間の増加や安全上の問題を生じること無く、繊維や繊維製品の洗濯において、洗浄効果を維持しながら、洗剤使用量を低減し、洗濯コストの節減を図ることができ、ガス溶解に関する特段の付帯設備を必要としないことにある。   The object of the present invention is to reduce the amount of detergent used and reduce the washing cost while maintaining the cleaning effect in washing of fibers and textile products without causing these problems, further increasing labor and safety problems. It is possible to save and no special incidental equipment for gas dissolution is required.

本発明の一態様は、密閉可能な洗濯槽を備えた洗濯機に係るもので、給水管、給水弁、給水圧力調整弁、排気管、排気弁、及び制御装置を備える。   One embodiment of the present invention relates to a washing machine including a sealable washing tub, and includes a water supply pipe, a water supply valve, a water supply pressure adjustment valve, an exhaust pipe, an exhaust valve, and a control device.

給水管は水道配管に接続されていて、該水道配管を流れる水道水を洗濯槽に供給するものである。給水弁は該給水管の流路を開閉可能である。給水圧力調整弁は、該給水管を通って該洗濯槽内に供給される水道水の圧力を調整可能である。排気管は、該洗濯槽内の気体を排気するものである。排気弁は、該排気管の流路を開閉可能である。制御装置は、該給水弁と該給水圧力調整弁と該排気弁を制御するものである。   The water supply pipe is connected to the water supply pipe and supplies the tap water flowing through the water supply pipe to the washing tub. The water supply valve can open and close the flow path of the water supply pipe. The water supply pressure adjustment valve can adjust the pressure of tap water supplied into the washing tub through the water supply pipe. The exhaust pipe exhausts the gas in the washing tub. The exhaust valve can open and close the flow path of the exhaust pipe. The control device controls the water supply valve, the water supply pressure adjustment valve, and the exhaust valve.

制御装置は、該洗濯槽を密閉した状態で該給水弁を開くことで水道の供給圧力によって水道水を該洗濯槽内に導入し、かつ、該給水圧力調整弁と該排気弁を制御して水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように該洗濯槽内の水に該洗濯槽内の空気を溶解させる。   The control device opens the water supply valve in a state where the washing tub is sealed to introduce tap water into the washing tub by a water supply pressure, and controls the water supply pressure adjusting valve and the exhaust valve. The air in the washing tub is dissolved in the water in the washing tub so that the total dissolved gas concentration in the water is 120% or more of the saturation solubility under atmospheric pressure.

他の態様は、水道水を用いて洗濯槽内の洗濯物を洗う洗濯方法であって、該洗濯槽内に洗濯物を投入した後、該洗濯槽を密閉した状態で水道の供給圧力によって水道水を該洗濯槽内に導入し、かつ、該洗濯槽への水道水の導入圧と該洗濯槽内の圧力を制御して水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように該洗濯槽内の水に該洗濯槽内のガスを溶解させることを特徴とする。   Another aspect is a washing method for washing laundry in a washing tub using tap water, and after the laundry is put into the washing tub, the washing tub is sealed and the water supply is supplied by a water supply pressure. Water is introduced into the washing tub, and the pressure of tap water introduced into the washing tub and the pressure in the washing tub is controlled so that the total dissolved gas concentration in the water is 120% or more of the saturated solubility under atmospheric pressure. Thus, the gas in the washing tub is dissolved in the water in the washing tub.

更に本発明の態様について述べる。   Furthermore, the aspect of this invention is described.

本発明者は洗濯やすすぎにおよぼす溶存気体濃度の効果について調べた結果、浸漬、洗濯、すすぎなど、洗濯に使用する水として、大気圧下で密閉された洗濯槽内に水道水を導入し、その水道水の供給圧によって洗濯槽内を加圧しながら、洗濯槽内の水中の溶存ガス濃度(溶解ガス濃度や、ガス溶存率とも呼ばれる。)を大気圧下の飽和溶解度の120%以上に上昇させた後、浸漬、洗濯、すすぎなどの洗濯工程中に洗濯槽内の圧力を大気圧に開放することによって、過飽和となった溶存ガスを洗濯物の繊維内部、あるいは洗濯物表面で微細気泡として発生させ、その微細気泡によって汚れを浮き上がらせて効果的に除去することが出来、ガス溶解に関する特段の付帯設備を要することなく洗濯時間の短縮、洗剤使用量の低減などの効果があることを見いだし、鋭意検討を進め本発明に到達した。   As a result of investigating the effect of dissolved gas concentration on washing and rinsing, the inventor introduced tap water into a washing tub sealed under atmospheric pressure as water used for washing, such as immersion, washing, and rinsing. While pressurizing the inside of the washing tub with the supply pressure of the tap water, the dissolved gas concentration in the washing tub water (also called dissolved gas concentration or gas dissolved rate) is increased to 120% or more of the saturation solubility under atmospheric pressure. Then, by releasing the pressure in the washing tub to atmospheric pressure during the washing process such as dipping, washing, rinsing, etc., the supersaturated dissolved gas becomes fine bubbles inside the laundry fibers or on the laundry surface. It can be generated and effectively removed by raising the dirt by the fine bubbles, and it has the effect of shortening the washing time and reducing the amount of detergent used without requiring special incidental equipment for gas dissolution As a result, the inventors have intensively studied to arrive at the present invention.

本発明でいう洗濯は、通常云われるところの洗濯、即ち、繊維状物品、皮革、毛皮、羽毛、獣毛、またはこれらからなる製品や、これらの性状を持つ人工的製品の洗浄をいい、また、染色等の後の洗浄や動物、鳥類などの生物の洗浄も含む。これらの中で、繊維および繊維製品に対して特に有効である。本発明は、洗濯用液体として水を使用するものに関し、洗剤類と一緒に使用するものだけなく、水洗いも含まれる。   The term “laundry” as used in the present invention refers to usual laundry, that is, washing of fibrous articles, leather, fur, feathers, animal hair, or products made of these, or artificial products having these properties. In addition, washing after dyeing and the like and washing of animals such as animals and birds are also included. Among these, it is particularly effective for fibers and textile products. The present invention relates to the use of water as a washing liquid, and includes washing with water as well as those used with detergents.

本発明でいう洗濯に使用される水としては、例えば浸漬用水、予洗用水、洗濯用水、すすぎ用水などとして使用される水を言う。本発明においては、浸漬、予洗、洗濯、浸漬等の操作のいずれか一つ、または複数の操作に於いて、密閉された洗濯槽へ水道水を導入し、その水道供給圧によって溶存ガス濃度を高めた水が使用される。   The water used for washing in the present invention refers to water used as, for example, immersion water, prewash water, laundry water, rinse water, and the like. In the present invention, in any one or a plurality of operations such as dipping, prewashing, washing, dipping, etc., tap water is introduced into a sealed washing tub, and the dissolved gas concentration is adjusted by the water supply pressure. Increased water is used.

溶存ガス濃度を高めた水とは、水中の全溶存ガス濃度が大気圧下における飽和溶解度の120%以上となるように洗濯槽内のガスが加圧溶解された水である。ガスとは、常温常圧において気体で存在する物質を指し、例えば、酸素、窒素、二酸化炭素、オゾン、塩素、水素、希ガス類などを例示することができる。複数の種類のガスの混合ガス(空気を含む。)を用いる場合には、該混合ガスの大気圧下における各成分ガスの各分圧における飽和溶解度の120%以上になるように各成分ガスが加圧溶解された水を用いる。オゾン、塩素などの酸化性ガスを使用した場合には、後述する圧力開放による気泡発生がもたらす洗浄効果に加えて、酸化力による殺菌、漂白などの洗浄効果も得ることができる。しかしながら、入手の容易さ、コスト、安全性から、本発明で使用するガスとしては空気(窒素約80%、酸素約20%)が望ましい。例えば、空気が大気圧、25℃の場合の溶存窒素飽和溶解度は約14mg/l、溶存酸素飽和溶解度は約8mg/lである。ガスの水への溶解度はヘンリーの法則に従うので、絶対圧1.2気圧以上とすれば、ガス飽和溶解度は大気圧下のときの120%以上となり、当該ガス溶解水は、後述するように浸漬、予洗、洗濯、すすぎなどの洗濯工程において、圧力を開放することにより洗濯物の繊維内部で微細気泡を発生し、汚れを浮き上がらせて良好な洗浄効果を得ることができる。   The water whose dissolved gas concentration is increased is water in which the gas in the washing tub is pressure-dissolved so that the total dissolved gas concentration in water is 120% or more of the saturation solubility under atmospheric pressure. The gas refers to a substance that exists as a gas at normal temperature and pressure, and examples thereof include oxygen, nitrogen, carbon dioxide, ozone, chlorine, hydrogen, and rare gases. In the case of using a mixed gas (including air) of a plurality of types of gases, each component gas must be 120% or more of the saturation solubility at each partial pressure of each component gas under the atmospheric pressure of the mixed gas. Use water dissolved under pressure. When an oxidizing gas such as ozone or chlorine is used, cleaning effects such as sterilization and bleaching by oxidizing power can be obtained in addition to the cleaning effect caused by the generation of bubbles by releasing the pressure described later. However, air (about 80% nitrogen and about 20% oxygen) is desirable as the gas used in the present invention because of its availability, cost, and safety. For example, when the air is at atmospheric pressure and 25 ° C., the dissolved nitrogen saturation solubility is about 14 mg / l, and the dissolved oxygen saturation solubility is about 8 mg / l. Since the solubility of gas in water follows Henry's law, if the absolute pressure is 1.2 atmospheres or more, the gas saturation solubility will be 120% or more at atmospheric pressure, and the gas-dissolved water will be immersed and prewashed as described later. In the washing process such as washing and rinsing, by releasing the pressure, fine bubbles are generated inside the fibers of the laundry, and the dirt is lifted to obtain a good cleaning effect.

ガスを水に溶解させる方法としては、水中の溶存ガス濃度が大気圧下における飽和溶解度の120%以上となりうる方法であれば良く、例えば、コンプレッサーによる気体の加圧、ポンプによる水の加圧、水道の供給圧による加圧、一部を可動とした洗濯槽で気液共存密閉下において加圧溶解する方法、エゼクターによるガス溶解、加圧下の乱流によるガス溶解方法、またはこれらの方法を組み合わせた方法などを例示することができる。コンプレッサーによる気体の加圧、ポンプによる水の加圧、水道の供給圧による加圧では、密閉可能な構造の洗濯槽に、コンプレッサーによって加圧されたガスを吹き込むか、ポンプによって加圧された水を導入する。流体を噴射してその周囲の気体や液体を吸引する装置をエゼクターというが、ポンプによる加圧か、または水道の供給水圧で水をノズルより噴射し、周囲のガスを吸引してガスを水に溶解させることもできる。とりわけ本発明では、通常1〜7kg/cm2程度で供給される水道水を密閉された洗濯槽内に導入することで、水道の供給圧を利用して洗濯槽内のガスを洗濯槽内の水に加圧溶解する。水道水圧を利用する方法は、洗濯機としては洗濯槽内を加圧する設備を必要とせず、洗濯槽を耐圧構造にするだけで済むので、特に好適である。 As a method for dissolving the gas in water, any method can be used as long as the dissolved gas concentration in water can be 120% or more of the saturation solubility under atmospheric pressure, for example, pressurization of gas by a compressor, pressurization of water by a pump, Pressurization with water supply pressure, partly movable washing tub with gas-liquid co-sealing, gas dissolution with ejector, gas dissolution with turbulent flow under pressure, or a combination of these The method etc. can be illustrated. In pressurization of gas by a compressor, pressurization of water by a pump, and pressurization by water supply pressure, gas pressurized by a compressor is blown into a washing tub having a sealable structure, or water pressurized by a pump Is introduced. A device that ejects fluid and sucks the surrounding gas or liquid is called an ejector, but water is ejected from the nozzle by pump pressurization or water supply water pressure, and the surrounding gas is sucked into the water. It can also be dissolved. In particular, in the present invention, by introducing tap water normally supplied at about 1 to 7 kg / cm 2 into a sealed washing tub, the gas in the washing tub is supplied into the washing tub using the supply pressure of the water tap. Dissolve under pressure in water. The method using tap water pressure is particularly suitable because the washing machine does not require a facility for pressurizing the inside of the washing tub, and only requires the washing tub to have a pressure-resistant structure.

上記ガス溶解方法において、気液二相が接触している状態で水またはガスの流れによって乱流を形成すれば、ガスの溶解をより効率よく行うことが出来る。例えば、密閉された洗濯槽に水道水を導入し、水道の供給水圧によって洗濯槽内を加圧した状態で回転ドラム等で洗濯槽内の水を揺動させることで水とガスの接触効率を高めてガスを水に溶解させる方法を例示することが出来る。   In the gas dissolving method, if a turbulent flow is formed by the flow of water or gas while the gas-liquid two phases are in contact with each other, the gas can be dissolved more efficiently. For example, by introducing tap water into a closed washing tub and pressurizing the inside of the washing tub with the supply water pressure of the tap water, the water in the washing tub is swung with a rotating drum or the like to improve the contact efficiency between water and gas. A method of increasing the gas and dissolving the gas in water can be exemplified.

本発明の洗濯機では、浸漬、予洗、洗濯、すすぎなどの洗濯工程で、ガス加圧溶解の際と同等の圧力で洗濯物と水が接触して保持された後、洗濯槽につながる配管に設けられた圧力開放弁が開放されて大気圧となることにより、当該水において過飽和となった溶存ガスが洗濯物の繊維内部、あるいは洗濯物表面で微細気泡として発生し、気泡によって汚れを浮き上がらせて効果的に除去することができる。前記圧力の保持は、ガスの溶解平衡を保持するため、洗濯槽内に気液二相が存在する状態で行われることが望ましい。また、圧力開放弁が洗濯槽内の液相側に設置されると、圧力開放の際に水を排出してしまうので好ましくない。圧力開放用の弁は、前記洗濯槽内の気相側に設置され、気体の排出によって洗濯槽の内圧が大気圧へと開放されることが望ましい。   In the washing machine of the present invention, in the washing process such as dipping, pre-washing, washing, rinsing, etc., the laundry and water are kept in contact with each other at the same pressure as in the gas pressure dissolution, and then connected to the washing tub. When the pressure release valve provided is opened to atmospheric pressure, dissolved gas supersaturated in the water is generated as fine bubbles inside the laundry fibers or on the surface of the laundry, causing the bubbles to raise dirt. Can be effectively removed. The pressure is preferably maintained in a state where a gas-liquid two phase exists in the washing tub in order to maintain a gas dissolution equilibrium. Moreover, if the pressure release valve is installed on the liquid phase side in the washing tub, water is discharged when the pressure is released, which is not preferable. The pressure release valve is preferably installed on the gas phase side in the washing tub, and the internal pressure of the washing tub is released to atmospheric pressure by discharging the gas.

飽和溶存ガス濃度は、溶解時の圧力を上昇させればヘンリーの法則にしたがって上昇し、圧力開放時のガス発生量も多くなるので、より良好な洗浄効果が得られる傾向にある。しかしながら、高圧に耐えうる洗濯槽は費用が嵩む。水中の溶存ガス濃度が大気圧下の飽和溶解度の120%を超えていれば一定の洗浄効果は得られるので、水中の溶存ガス濃度の下限を大気圧下の飽和溶解度の120%とし、その上限は費用、安全性等を総合的に考慮して決定することが好ましい。   The saturated dissolved gas concentration increases according to Henry's law if the pressure at the time of dissolution is increased, and the amount of gas generated when the pressure is released increases, so that a better cleaning effect tends to be obtained. However, a washing tub that can withstand high pressure is expensive. If the dissolved gas concentration in water exceeds 120% of the saturation solubility under atmospheric pressure, a certain cleaning effect can be obtained, so the lower limit of the dissolved gas concentration in water is 120% of the saturation solubility under atmospheric pressure, and the upper limit Is preferably determined in consideration of cost, safety and the like.

上述した、大気圧への圧力変動による微細気泡発生に続いて、洗濯槽をさらに減圧して水中の全溶存ガス濃度を大気圧下の飽和溶解度の80%以下とし、洗濯物の繊維内部、あるいは洗濯物表面での微細気泡発生を促進させることで、より強力な汚れ除去効果を得ることができる。水中の溶存ガス濃度を大気圧下の飽和溶解度の80%以下とするには、絶対圧0.8気圧(608mmHg)以下の真空度とすれば良く、真空ポンプやエゼクターによる減圧で容易に達成することができる。真空度を絶対圧0.8気圧(608mmHg)より更に下げればより多くの気泡を発生させることは可能ではある。しかし、増加する気泡量はわずかであるため、洗濯槽の真空度の上限は水中の溶存ガス濃度が大気圧下の飽和溶解度の80%となる真空度とし、その下限は洗濯槽の耐真空性にかかる費用などを総合的に考慮して決定することが好ましい。   Following the generation of fine bubbles due to pressure fluctuations to atmospheric pressure as described above, the laundry tub is further depressurized so that the total dissolved gas concentration in the water is 80% or less of the saturated solubility under atmospheric pressure, inside the fibers of the laundry, or By promoting the generation of fine bubbles on the surface of the laundry, a more powerful dirt removal effect can be obtained. In order to make the dissolved gas concentration in water 80% or less of the saturation solubility under atmospheric pressure, the absolute pressure should be 0.8 atm (608mmHg) or less, which can be easily achieved by depressurization with a vacuum pump or ejector. it can. It is possible to generate more bubbles if the degree of vacuum is further reduced below the absolute pressure of 0.8 atm (608 mmHg). However, since the amount of bubbles to increase is small, the upper limit of the vacuum level of the washing tub is the vacuum level at which the dissolved gas concentration in water is 80% of the saturated solubility under atmospheric pressure, and the lower limit is the vacuum resistance of the washing tub. It is preferable to determine the cost in consideration of the total cost.

本発明の洗濯機においては、微細気泡の発生が繊維内部の汚れを浮き上がらせて除去できるので、洗剤の使用量を大幅に低減することができる。一般に洗剤は、一定量以上使用しても洗浄効果が使用量に応じて良くなり続けるものではない。過剰な洗剤の使用は、洗剤を無駄にするだけでなく、排水による環境負荷を増大させ、またより多くのすすぎ水を必要とするなど、デメリットが大きい。そこで、洗剤には適正な使用量を示す標準使用量が定められているが、本発明の洗濯機では、微細気泡が洗浄効果を補助するので、後述の実施例で例示するように、洗剤使用量を標準使用量の1/3以下としても、従来の洗濯機において標準使用量を用いた場合と同等の洗浄効果を得ることができる。   In the washing machine of the present invention, the generation of fine bubbles can lift and remove dirt inside the fiber, so that the amount of detergent used can be greatly reduced. In general, detergents do not continue to improve the cleaning effect according to the amount used, even if they are used above a certain amount. The use of an excessive amount of detergent not only wastes the detergent, but also increases the environmental load due to drainage, and requires more rinsing water. Therefore, a standard usage amount indicating an appropriate usage amount is set for the detergent. However, in the washing machine of the present invention, the fine bubbles assist the cleaning effect. Even if the amount is 1/3 or less of the standard use amount, a cleaning effect equivalent to the case of using the standard use amount in a conventional washing machine can be obtained.

また、本発明の洗濯機において、浸漬、予洗、洗濯、すすぎなどの洗濯工程に用いるガスを溶解させる水を、硬度50mgCaCO3/l以下の軟水とすれば、洗剤の洗浄効果を高めることができる。硬度50mgCaCO3/lの軟水は、通常の軟化操作により得ることが出来る。即ち、Na形陽イオン交換樹脂(例えばロームアンドハース社製アンバーライト120b)の充填層に空間流速50h-1程度で原水を通水し、原水中の硬度成分をナトリウムイオンと交換させることにより軟水を得る。 Further, in the washing machine of the present invention, if the water used to dissolve the gas used in the washing process such as dipping, prewashing, washing, rinsing is soft water having a hardness of 50 mg CaCO 3 / l or less, the washing effect of the detergent can be enhanced. . Soft water having a hardness of 50 mg CaCO 3 / l can be obtained by a normal softening operation. In other words, raw water is passed through a packed bed of Na-type cation exchange resin (for example, Amberlite 120b manufactured by Rohm and Haas) at a space flow velocity of about 50h-1, and the hardness component in the raw water is exchanged with sodium ions for soft water. Get.

更に、本発明の洗濯機において、ガスを溶解させる水として、導電率100μS/cm以下、より好ましくは導電率50μS/cm以下の脱塩水を用いれば、更に洗剤の洗浄効果を高めることができる。水を脱塩する方法は特に限定されるものではなく、イオン交換樹脂や逆浸透膜を用いる方法を例示することが出来る。特開2010-29753号公報に開示されているような電気化学式脱イオン水製造装置を用いれば、イオン交換樹脂カートリッジや逆浸透膜モジュールの交換が不要となり好適である。   Furthermore, in the washing machine of the present invention, if demineralized water having a conductivity of 100 μS / cm or less, more preferably a conductivity of 50 μS / cm or less is used as water for dissolving the gas, the washing effect of the detergent can be further enhanced. The method for desalting water is not particularly limited, and a method using an ion exchange resin or a reverse osmosis membrane can be exemplified. Use of an electrochemical deionized water production apparatus as disclosed in Japanese Patent Application Laid-Open No. 2010-29753 is preferable because it is not necessary to replace an ion exchange resin cartridge or a reverse osmosis membrane module.

洗剤の主成分である界面活性剤は、親水部と疎水部よりなる分子構造を有し、汚れである油分を疎水部で疎水性相互作用によって補足しながら、同時に他方において親水部の水への親和性で水中に分散することにより、汚れを水中に安定分散させて水の排水とともに流出除去させる働きを有している。水中にイオン、中でもカルシウムやマグネシウムといった二価のイオンが存在すると、これらのイオンが界面活性剤の親水部と結合してしまい、界面活性剤の機能を著しく阻害する。このため、二価のカルシウムやマグネシウムイオンを一価のナトリウムイオンに交換した軟水を用いた場合、上述のように良好な洗浄効果を得ることができる。更に、水を脱塩し一価のイオンも除去した場合には、軟水に比べて更に界面活性剤の汚れ分散効果が高くなり、極めて良好な洗浄効果を得ることができる。
通常、市販されている洗剤には、イオンによる界面活性剤の阻害を防止するために、助剤(キレート剤)などが含まれている。軟水や脱塩水を用いた場合には、イオンによる界面活性剤の阻害がほとんどないので、助剤を含まない天然石鹸でも良好な洗浄効果を得ることができる。
The surfactant, the main component of the detergent, has a molecular structure consisting of a hydrophilic part and a hydrophobic part. By dispersing in water with affinity, it functions to stably disperse dirt in water and remove it with water drainage. When ions, especially divalent ions such as calcium and magnesium, are present in water, these ions bind to the hydrophilic portion of the surfactant, and the function of the surfactant is significantly inhibited. For this reason, when using soft water in which divalent calcium or magnesium ions are exchanged for monovalent sodium ions, a good cleaning effect can be obtained as described above. Further, when the water is desalted to remove monovalent ions, the effect of dispersing the surfactant with the soil is further enhanced as compared with soft water, and a very good cleaning effect can be obtained.
Usually, a commercially available detergent contains an auxiliary agent (chelating agent) or the like in order to prevent the surfactant from being inhibited by ions. When soft water or demineralized water is used, there is almost no inhibition of the surfactant by ions, so that a natural soap containing no auxiliary agent can provide a good cleaning effect.

本発明の洗濯機において、水道水導入時の加圧による水へのガス溶解、圧力開放弁の開放による大気圧への開放、その後必要に応じて行われる減圧は、浸漬、予洗、洗濯、すすぎなどの洗濯工程の少なくとも一部で、通常一回行われて良好な洗浄効果をもたらすが、汚れがひどい場合などは、前記加圧、大気開放、減圧のサイクルを必要回数繰り返すことにより、良好な洗浄効果を得ることができる。   In the washing machine of the present invention, gas dissolution into water by pressurization at the time of introduction of tap water, release to atmospheric pressure by opening a pressure release valve, and subsequent decompression as necessary are immersion, prewash, washing, rinsing In at least a part of the washing process, etc., it is usually performed once and brings about a good cleaning effect. However, when the dirt is severe, it is preferable to repeat the above pressurization, release to the atmosphere, and decompression cycles as many times as necessary. A cleaning effect can be obtained.

以上のように本発明では、大気圧下で密閉された洗濯槽内に水道水を導入し、その水道水の供給圧によって洗濯槽内を加圧することで、水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように洗濯槽内のガスを洗濯槽内の水に加圧溶解させた後、洗濯槽に設置された圧力開放弁を開放することによって、圧力解放後は当該水において過飽和となった溶存ガスを洗濯物の繊維内部、あるいは洗濯物表面で微細気泡として発生させ、該気泡によって汚れを浮き上がらせて除去することができる。更に洗濯槽を減圧して、水中の全溶存ガス濃度を大気圧下の飽和溶解度の80%以下とすることで、洗濯物の繊維内部、あるいは洗濯物表面での微細気泡発生を促進させ、より強力な汚れ除去効果を得ることができる。また、水道水圧を利用して水にガスを溶解させたことにより、洗濯機はガス溶解に関する特段の付帯設備が要らないため、洗濯機の価格を低く抑えることが出来る。   As described above, in the present invention, tap water is introduced into a washing tub sealed under atmospheric pressure, and the inside of the washing tub is pressurized by the supply pressure of the tap water, so that the total dissolved gas concentration in water is atmospheric pressure. After releasing the pressure by opening the pressure relief valve installed in the washing tub after pressure-dissolving the gas in the washing tub in the water in the washing tub so that it becomes 120% or more of the lower saturated solubility, The dissolved gas supersaturated in the water can be generated as fine bubbles inside the laundry fibers or on the surface of the laundry, and the bubbles can be lifted and removed by the bubbles. Furthermore, by depressurizing the washing tub and setting the total dissolved gas concentration in water to 80% or less of the saturated solubility under atmospheric pressure, the generation of fine bubbles inside the laundry fibers or on the laundry surface is promoted. A powerful dirt removal effect can be obtained. In addition, since the gas is dissolved in the water using the tap water pressure, the washing machine does not require special incidental facilities for gas dissolution, and thus the price of the washing machine can be kept low.

したがって本発明の洗濯機によれば、繊維や繊維製品の洗濯において、洗浄効果を維持しながら、洗剤使用量を低減し、洗濯コストの節減を図ることができ、ガス溶解に関する特段の付帯設備を必要としない。   Therefore, according to the washing machine of the present invention, it is possible to reduce the amount of detergent used and reduce the washing cost while maintaining the cleaning effect in the washing of fibers and textile products. do not need.

本発明の一実施例による洗濯機の構成要素を示す模式図である。It is a schematic diagram which shows the component of the washing machine by one Example of this invention.

以下、本発明の実施の形態について図面を参照して説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1に本実施例の洗濯機の構成を模式的に示す。図1によると、洗濯機1は洗濯槽2を有し、洗濯槽2は、水又は、洗剤等を含んだ水と一緒に洗濯物を回転させる回転ドラム3を備えている。さらに洗濯槽2は、水漏れだけでなく空気漏れしないように密閉できる構造を有する。例えば洗濯槽2には洗濯物の投入口を開閉できる蓋が設けられ、投入口と蓋の間にはパッキン等のシール部材および、その蓋で投入口が気密に閉じられた状態に蓋を固定するロック機構が設けられている。   FIG. 1 schematically shows the configuration of the washing machine of this embodiment. According to FIG. 1, the washing machine 1 has a washing tub 2, and the washing tub 2 includes a rotating drum 3 that rotates the laundry together with water or water containing a detergent or the like. Furthermore, the washing tub 2 has a structure that can be sealed so that not only water leakage but also air leakage does not occur. For example, the laundry tub 2 is provided with a lid capable of opening and closing the laundry inlet, and a seal member such as packing is provided between the inlet and the lid, and the lid is fixed in a state where the inlet is hermetically closed by the lid. A locking mechanism is provided.

洗濯槽2の上部には、水道水を洗濯槽内2に供給する給水管4、及び洗濯槽内6の気体を排出する排気管6がそれぞれ別個に接続されている。給水管4の洗濯機1より上流側端は水道蛇口、もしくは水道配管の水取り出し弁とつながっており、洗濯機1の内部においては給水管4には、給水圧力を調整する給水圧力調整弁7、及び給水管4の流路を開閉する給水弁8が設置されている。さらに洗濯機1の内部において排気管6には、排気管6の流路を開閉する排気弁6が設置されている。   A water supply pipe 4 for supplying tap water to the inside of the washing tub 2 and an exhaust pipe 6 for discharging the gas in the washing tub 6 are separately connected to the upper part of the washing tub 2. The upstream end of the water supply pipe 4 from the washing machine 1 is connected to a water faucet or a water outlet valve of the water pipe. Inside the washing machine 1, the water supply pipe 4 has a water supply pressure adjusting valve 7 for adjusting the water supply pressure. And the water supply valve 8 which opens and closes the flow path of the water supply pipe 4 is installed. Further, an exhaust valve 6 that opens and closes the flow path of the exhaust pipe 6 is installed in the exhaust pipe 6 inside the washing machine 1.

洗濯槽2の底部には、洗濯槽2内の水又は、洗剤等を含んだ水を洗濯機1の外へ排出する排水管5が接続されている。さらに洗濯機1の内部において排水管5には、排水管5の流路を開閉する排水弁9が設置されている。   Connected to the bottom of the washing tub 2 is a drain pipe 5 that discharges the water in the washing tub 2 or water containing a detergent to the outside of the washing machine 1. Furthermore, a drain valve 9 that opens and closes the flow path of the drain pipe 5 is installed in the drain pipe 5 inside the washing machine 1.

上記回転ドラム3、給水圧力調整弁7、給水弁8、排水弁9、及び排気弁10は不図示の制御装置との電気信号の授受により制御されるようになっている。   The rotary drum 3, the feed water pressure adjusting valve 7, the feed water valve 8, the drain valve 9 and the exhaust valve 10 are controlled by sending and receiving electrical signals with a control device (not shown).

本実施例の洗濯機1で洗濯する場合は、洗濯槽2に洗濯物を投入した後、洗濯物投入口を蓋で密閉し、排水弁9及び排気弁10を閉じ、給水弁8のみを開けておく。尚、この洗濯物投入口の密閉並びに排水弁9及び排気弁10の閉操作後に空気以外のガス(オゾン、塩素など)を洗濯槽内2に導入しても良いが、コストと安全性から本実施例ではそのようなガスを導入していない。   In the case of washing with the washing machine 1 of this embodiment, after the laundry is put into the washing tub 2, the laundry inlet is sealed with a lid, the drain valve 9 and the exhaust valve 10 are closed, and only the water supply valve 8 is opened. Keep it. In addition, after closing the laundry inlet and closing the drain valve 9 and the exhaust valve 10, gases other than air (ozone, chlorine, etc.) may be introduced into the washing tub 2. In the embodiment, such a gas is not introduced.

次いで、水道蛇口もしくは、水道配管の水取り出し弁を開き、水道水を給水管4によって洗濯槽2内へ導入する。この水道水導入中においては、給水圧力調整弁7により所定の給水圧力(ゲージ圧0.02MPa(絶対圧0.12MPa)以上の固定値)とした水道水を導入し、かつ、洗濯槽2内が所定の圧力(ゲージ圧0.02MPa(絶対圧0.12MPa)以上の固定値)及び所定の水量になるように排気弁10の開閉を適宜行う。これにより、水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように洗濯槽内のガス(空気)が洗濯槽内の水に加圧溶解する。   Next, the tap or the water take-off valve of the water pipe is opened, and the tap water is introduced into the washing tub 2 through the water supply pipe 4. During the introduction of tap water, tap water at a predetermined feed water pressure (fixed value of gauge pressure 0.02 MPa (absolute pressure 0.12 MPa) or higher) is introduced by the feed water pressure adjusting valve 7 and the inside of the washing tub 2 is predetermined. The exhaust valve 10 is appropriately opened and closed so that the pressure becomes (a fixed value of gauge pressure 0.02 MPa (absolute pressure 0.12 MPa) or higher) and a predetermined amount of water. As a result, the gas (air) in the washing tub is pressure-dissolved in the water in the washing tub so that the total dissolved gas concentration in the water is 120% or more of the saturation solubility under atmospheric pressure.

その後、給水弁8を閉じ、回転ドラム3を回転又は揺動させて洗濯槽2内の水相と気相を混合させる。これにより、洗濯槽2内において空気の水への溶解が促進される。   Thereafter, the water supply valve 8 is closed, and the rotating drum 3 is rotated or swung to mix the water phase and the gas phase in the washing tub 2. Thereby, dissolution of air into water is promoted in the washing tub 2.

続いて、回転ドラム3の回転を一旦停止し、排気弁6のみを開いて洗濯槽2内を大気圧に開放する。これにより、水において過飽和となった溶存ガス(酸素と窒素が主な成分である空気)を洗濯物の繊維内部、あるいは洗濯物表面で微細気泡として発生させ、該気泡によって汚れを浮き上がらせて除去することができる。   Subsequently, the rotation of the rotary drum 3 is temporarily stopped, only the exhaust valve 6 is opened, and the inside of the washing tub 2 is opened to atmospheric pressure. As a result, dissolved gas that is supersaturated in water (air containing oxygen and nitrogen as main components) is generated as fine bubbles inside the laundry fibers or on the surface of the laundry, and the bubbles lift and remove dirt. can do.

しかる後、再び回転ドラム3により洗濯槽1内の洗濯物を回転させて洗う。   After that, the laundry in the washing tub 1 is rotated again by the rotating drum 3 and washed.

以上の操作により洗濯工程が行われるが、すすぎ工程においても洗濯工程と操作は同じである。   Although the washing process is performed by the above operation, the washing process and the operation are the same in the rinsing process.

なお、上記説明では水中に微細気泡を発生させるのに排気弁6を開いて洗濯槽2内を大気圧に開放しているが、より多くの微細気泡発生の為には、排気弁6を閉じた状態で洗濯槽2内を大気圧以下に減圧することが好ましい。このため、排気管6には、洗濯槽内2を大気圧以下に減圧する(即ち負圧にする)真空ポンプやエグゼクター等の減圧装置が取り付けられていると良い。   In the above description, the exhaust valve 6 is opened and the inside of the washing tub 2 is opened to atmospheric pressure in order to generate fine bubbles in water. However, in order to generate more fine bubbles, the exhaust valve 6 is closed. It is preferable that the inside of the washing tub 2 is depressurized to an atmospheric pressure or lower in the state where For this reason, the exhaust pipe 6 is preferably provided with a decompression device such as a vacuum pump or an executor for decompressing the inside of the washing tub 2 to an atmospheric pressure or lower (that is, a negative pressure).

また、洗剤の洗浄効果を高める為には、図1に示すように、洗濯槽2に供給される水道水を硬度50mgCaCO3/l以下の軟水にする軟水化装置11、又は/及び、当該水道水を導電率100μS/cm以下、より好ましくは導電率50μS/cm以下の脱塩水にする脱塩装置12が給水管4に取り付けられていると良い。しかし、洗濯機がこのような軟水化装置や脱塩装置を具備しなくても本願の課題は解決される。 In addition, in order to enhance the cleaning effect of the detergent, as shown in FIG. 1, the water softening device 11 for making tap water supplied to the washing tub 2 soft water having a hardness of 50 mg CaCO 3 / l or less, and / or the tap water A desalinator 12 that converts water into desalted water having a conductivity of 100 μS / cm or less, more preferably a conductivity of 50 μS / cm or less, is preferably attached to the water supply pipe 4. However, even if the washing machine does not include such a water softening device or a desalination device, the problem of the present application is solved.

なお、軟水化装置としては例えば、Na形陽イオン交換樹脂(例えばロームアンドハース社製アンバーライト120b)の充填層に通水させる装置を適用できる。脱塩装置としては例えば、イオン交換樹脂や逆浸透膜、あるいは特開2010-29753号公報に開示されているような電気化学式脱イオン水製造装置を適用できる。   As the water softening device, for example, a device for passing water through a packed bed of Na-type cation exchange resin (for example, Amberlite 120b manufactured by Rohm and Haas) can be applied. As the desalting apparatus, for example, an ion exchange resin, a reverse osmosis membrane, or an electrochemical deionized water production apparatus as disclosed in JP 2010-29753 A can be applied.

JIS C9811「家庭用電気洗濯機の性能測定方法」に従って本発明の洗濯機の洗浄効果を確認した。以下、そのための実施例を示す。   The washing effect of the washing machine of the present invention was confirmed according to JIS C9811 “Performance measurement method for household electric washing machine”. Examples for this purpose will be shown below.

(実施例1)
a)洗濯槽について
ステンレス製で内径100mmの円筒形の密閉可能な容量1.2リットルの容器を作製し洗濯槽とした。洗濯槽の直胴部中央付近に外径3mmのステンレス配管を円周方向に6cm離して2本接続し、該配管にそれぞれ一個のステンレス製バルブを配設して、一つを水導入弁、他方をガス排出弁とした。水導入弁は、圧力調整弁(いわゆる減圧弁)と該圧力調整弁の下流側に圧力計を配設した配管を通じて水道蛇口に接続され、洗濯槽に水道水を該圧力調整弁で設定した所定の圧力で導入する際に開として用いた。ガス排出弁は、洗濯槽への水導入時に必要に応じて開として適宜洗濯槽内の空気を排出し、前記所定の圧力で後述の所定の洗濯水量(600ml)を洗濯槽内に導入するよう調整した。また、ガス排出弁は、洗濯槽内の圧力を開放して大気圧とする際にも開として用いた。用いた水道水の導電率は250μS/cm、硬度は80mgCaCO3/lであった。
Example 1
a) Washing tub A cylindrical container with a capacity of 1.2 liters made of stainless steel and having an inner diameter of 100 mm was prepared as a washing tub. Two stainless steel pipes with an outer diameter of 3 mm are connected 6 cm apart in the circumferential direction near the center of the straight body of the washing tub, one stainless steel valve is arranged on each pipe, one is a water introduction valve, The other was a gas discharge valve. The water introduction valve is connected to a water tap through a pressure regulating valve (so-called pressure reducing valve) and a pipe provided with a pressure gauge downstream of the pressure regulating valve, and tap water is set in the washing tub with the pressure regulating valve. It was used as open when introduced at a pressure of. The gas discharge valve is opened as necessary when water is introduced into the washing tub so that air in the washing tub is appropriately discharged, and a predetermined washing water amount (600 ml) described later is introduced into the washing tub at the predetermined pressure. It was adjusted. The gas discharge valve was also used as open when the pressure in the washing tub was released to atmospheric pressure. The tap water used had a conductivity of 250 μS / cm and a hardness of 80 mg CaCO 3 / l.

b)洗濯物について
本実施例で使用される洗濯物としては、JIS C9811附属書3で規定されている汚染布を財団法人洗濯科学協会が調製頒布しているもの(5cm×5cm)を購入して用いた。
b) Laundry For the laundry used in this example, purchase one (5cm x 5cm) that is prepared and distributed by the Laundry Science Association of the contaminated cloth specified in JIS C9811 Annex 3. Used.

c)洗濯工程について
洗濯槽に汚染布3 枚と市販洗剤(花王ニュービーズ:標準使用量25g/30リットル)を水600mlに対して標準使用量の1/3となるように投入した。次に前記圧力調整弁によって給水圧0.02MPa(ゲージ圧)とした水道水を洗濯槽内に導入し、洗濯槽内の圧力がゲージ圧0.02MPa(絶対圧0.12MPa)、水量が600mlとなるように前記ガス排出弁を適宜開として洗濯槽内の空気を排出しながら洗濯槽に水を張り込んだ。水導入弁、ガス排出弁を閉として洗濯槽を密閉状態とし、洗濯槽を振とう機に取り付け25℃で10分間振とうした。次に、一旦振とうを停止してガス排出弁を開とし、洗濯槽内の圧力を大気圧とした後、再度ガス排出弁を閉として更に5分間振とうした。
c) Laundry process Three contaminated cloths and a commercial detergent (Kao New Beads: standard usage 25g / 30 liters) were put into the washing tub so that it would be 1/3 of the standard usage for 600ml of water. Next, tap water with a water supply pressure of 0.02 MPa (gauge pressure) is introduced into the washing tub by the pressure adjusting valve so that the pressure in the washing tub is 0.02 MPa (absolute pressure 0.12 MPa) and the water volume is 600 ml. Then, the gas discharge valve was opened as appropriate, and water was poured into the washing tub while discharging air in the washing tub. The water introduction valve and the gas discharge valve were closed to close the washing tub, and the washing tub was attached to a shaker and shaken at 25 ° C. for 10 minutes. Next, shaking was stopped once, the gas discharge valve was opened, the pressure in the washing tub was set to atmospheric pressure, the gas discharge valve was closed again, and the mixture was shaken for another 5 minutes.

d)すすぎ工程について
前記洗濯の後、洗濯槽内の水を排出して洗濯工程と同様に水道水600mlを導入して洗濯槽内の圧力をゲージ圧0.02MPa(絶対圧0.12MPa)とした。洗濯槽を振とう機に取り付け室温で5分間振とうし、一旦振とうを停止してガス排出弁を開とし、洗濯槽内の圧力を大気圧とした後、再度ガス導入排出弁を閉として更に5分間振とうした。前記のような加圧状態で5分間、大気開放で5分間の振とうを再度行い、合計20分間の振とうをすすぎ工程とした。
d) Rinsing step After the washing, the water in the washing tub was drained and 600 ml of tap water was introduced in the same manner as the washing step, and the pressure in the washing tub was set to a gauge pressure of 0.02 MPa (absolute pressure 0.12 MPa). Attach the washing tub to the shaker, shake at room temperature for 5 minutes, stop shaking once, open the gas discharge valve, set the pressure in the washing tub to atmospheric pressure, and then close the gas introduction / discharge valve again Shake for another 5 minutes. Shaking for 5 minutes in the pressurized state as described above and 5 minutes in the open atmosphere was performed again, and shaking for a total of 20 minutes was used as a rinsing step.

e)乾燥工程について
汚染布を洗濯槽より取り出して室温で4時間放置乾燥後、アイロンをかけて乾燥させた。
e) About the drying process The contaminated cloth was taken out of the washing tub and left to dry at room temperature for 4 hours, and then dried with an iron.

f)残留汚れの評価について
乾燥させた汚染布の残留汚れを日立製表面反射率測定装置U-3010を用いて波長535 nmでの表面反射率を測定し、下式によって残留汚れ(%)を算出して洗浄効果を評価した。
残留汚れ(%) = 試験前の汚染布の反射率(%) − 試験後の汚染布の反射率(%)
(実施例2)
洗濯とすすぎ工程での水道水導入時の圧力をゲージ圧0.05MPa(絶対圧0.15MPa)とした以外は、実施例1と同様に操作して残留汚れを評価し実施例2とした。
f) Evaluation of residual dirt Measure the surface reflectance at a wavelength of 535 nm using a surface reflectance measuring device U-3010 made by Hitachi and measure the residual dirt (%) using the following formula. The cleaning effect was evaluated by calculation.
Residual stain (%) = Reflection of contaminated fabric before test (%) − Reflectivity of contaminated fabric after test (%)
(Example 2)
Residual dirt was evaluated in the same manner as in Example 1 except that the pressure at the time of introducing tap water in the washing and rinsing steps was changed to a gauge pressure of 0.05 MPa (absolute pressure of 0.15 MPa).

(実施例3)
洗濯とすすぎ工程での水道水導入時の圧力をゲージ圧0.10MPa(絶対圧0.20MPa)とした以外は、実施例1と同様に操作して残留汚れを評価し実施例3とした。本実施例では、水道水導入時にガス排出弁を開として水量を調整することなく、洗濯槽内をゲージ圧0.10MPa(絶対圧0.20MPa)として約600mlの水を張り込むことができた。水への空気の溶解により、本実施例では水量は600mlを約20ml上回ったが、わずかな違いであるので、他の実施例、比較例と同様に評価した。
(Example 3)
Example 3 was carried out in the same manner as in Example 1 except that the pressure at the time of introducing tap water in the washing and rinsing steps was changed to a gauge pressure of 0.10 MPa (absolute pressure of 0.20 MPa) to evaluate residual dirt. In this example, it was possible to inject about 600 ml of water into the washing tub with a gauge pressure of 0.10 MPa (absolute pressure of 0.20 MPa) without opening the gas discharge valve and adjusting the amount of water when introducing tap water. Due to the dissolution of air in water, the amount of water in this example exceeded about 20 ml over 600 ml, but this was a slight difference and was evaluated in the same manner as the other examples and comparative examples.

(実施例4)
洗濯とすすぎ工程での大気開放に続けて、エゼクターをガス排出弁に接続し、洗濯槽内の圧力を絶対圧600mmHgの負圧とし、実施例1では大気圧下で行なわれた大気開放後の5分間の洗濯とすすぎを減圧下で行なった以外は実施例1と同様に操作して残留汚れを評価し、実施例4とした。
Example 4
Following the opening of the atmosphere in the washing and rinsing process, the ejector is connected to the gas discharge valve, and the pressure in the washing tub is set to a negative pressure of 600 mmHg. In Example 1, after the opening of the atmosphere performed at atmospheric pressure. Residual stains were evaluated in the same manner as in Example 1 except that washing and rinsing for 5 minutes were performed under reduced pressure.

(実施例5)
洗濯とすすぎ工程での大気開放に続けて、エゼクターをガス排出弁に接続し、洗濯槽内の圧力を絶対圧100mmHgの負圧とし、実施例1では大気圧下で行なわれた大気開放後の5分間の洗濯とすすぎを減圧下で行なった以外は実施例1と同様に操作して残留汚れを評価し、実施例5とした。
(Example 5)
Following the air release in the washing and rinsing process, the ejector is connected to the gas discharge valve, and the pressure in the washing tub is set to a negative pressure of 100 mmHg. Residual dirt was evaluated in the same manner as in Example 1 except that washing and rinsing for 5 minutes were performed under reduced pressure.

(実施例6)
洗濯とすすぎ工程で使用する水を、水道水をNa形陽イオン交換樹脂に通水し軟化処理して得た軟水と水道水原水をブレンドすることにより、硬度50mgCaCO3/lとした以外は、実施例1と同様に操作して残留汚れを評価し実施例6とした。
(Example 6)
The water used in the washing and rinsing process is made by blending soft water obtained by passing tap water through a Na-type cation exchange resin and softening it, and tap water raw water, so that the hardness is 50 mg CaCO 3 / l. The operation was performed in the same manner as in Example 1 to evaluate residual dirt, and Example 6 was obtained.

(実施例7)
洗濯とすすぎ工程で使用する水を、水道水をH形陽イオン交換樹脂とOH形陰イオン交換樹脂の等体積混合層に通水して脱塩して得た純水と水道水原水をブレンドすることにより、導電率50μS/cmとした以外は、実施例1と同様に操作して残留汚れを評価し実施例7とした。
(Example 7)
The water used in the washing and rinsing process is blended with pure water obtained by desalting by passing tap water through an equal volume mixed layer of H-type cation exchange resin and OH-type anion exchange resin and tap water raw water Thus, except that the conductivity was set to 50 μS / cm, the residual dirt was evaluated in the same manner as in Example 1 to obtain Example 7.

(比較例1)
洗濯とすすぎ工程で水道水張り込み時にガス排出弁を開として、水道水圧による加圧を行なわず、洗濯とすすぎ工程の全てを大気圧下で行なった以外は、実施例1と同様に操作して残留汚れを評価し、比較例1とした。
(Comparative Example 1)
The same operation as in Example 1 was carried out except that the gas discharge valve was opened at the time of filling with tap water in the washing and rinsing process, and the pressurization by tap water pressure was not performed, and all the washing and rinsing processes were performed at atmospheric pressure. Residual dirt was evaluated and it was set as Comparative Example 1.

(溶存ガス濃度の確認)
上述の実施例1〜7、比較例1において、圧力調整によって溶存ガスがヘンリーの法則に従って調整されていたことを以下の手順で確認した。洗濯槽に水道水600mlのみを入れ、ガス排出弁に空気ボンベを接続して洗濯槽内の圧力をゲージ圧0.00(大気圧)、0.02、0.05、0.10MPa(絶対圧0.10、0.12、0.15、0.20MPa)とするか、または実施例4、5に記載されたと同様の方法で洗濯槽内の圧力を絶対圧600、100mmHgの負圧とする。そして洗濯槽を25℃で振とう機で5分間振とうした後、溶存酸素濃度と溶存窒素濃度をオービスフェア社製3625型溶存ガス測定装置で測定した。結果を表1に示した。溶存酸素濃度と溶存窒素濃度は、絶対圧に比例し±10%以内の範囲でヘンリーの法則に従っていた。
(Confirmation of dissolved gas concentration)
In Examples 1 to 7 and Comparative Example 1 described above, it was confirmed by the following procedure that the dissolved gas was adjusted according to Henry's law by pressure adjustment. Put only 600ml of tap water in the washing tub, connect an air cylinder to the gas discharge valve and adjust the pressure in the washing tub to gauge pressure 0.00 (atmospheric pressure), 0.02, 0.05, 0.10MPa (absolute pressure 0.10, 0.12, 0.15, 0.20) MPa), or the pressure in the washing tub is set to a negative pressure of 600 mm and 100 mmHg in the same manner as described in Examples 4 and 5. The washing tub was shaken with a shaker at 25 ° C. for 5 minutes, and then the dissolved oxygen concentration and the dissolved nitrogen concentration were measured with a 3625 type dissolved gas measuring device manufactured by Orbis Fair. The results are shown in Table 1. The dissolved oxygen concentration and the dissolved nitrogen concentration were proportional to the absolute pressure and obeyed Henry's law within a range of ± 10%.

Figure 2014068798
Figure 2014068798

実施例1〜7および比較例1の結果を表2に示した。残留汚れ(%)は、3枚の汚染布の平均値を示した。 The results of Examples 1 to 7 and Comparative Example 1 are shown in Table 2. Residual stain (%) showed the average value of the three soiled cloths.

Figure 2014068798
Figure 2014068798

1 洗濯機
2 洗濯槽
3 回転ドラム
4 給水管
5 排水管
6 排気管
7 給水圧力調整弁
8 給水弁
9 排水弁
10 排気弁
DESCRIPTION OF SYMBOLS 1 Washing machine 2 Washing tub 3 Rotating drum 4 Water supply pipe 5 Drain pipe 6 Exhaust pipe 7 Water supply pressure adjustment valve 8 Water supply valve 9 Drain valve 10 Exhaust valve

Claims (14)

密閉可能な洗濯槽を備えた洗濯機であって、
水道配管に接続され、該水道配管を流れる水道水を前記洗濯槽に供給する給水管と、前記給水管の流路を開閉する給水弁と、前記給水管を通って前記洗濯槽内に供給される水道水の圧力を調整する給水圧力調整弁と、前記洗濯槽内の気体を排気する排気管と、前記排気管の流路を開閉する排気弁と、前記給水弁と前記給水圧力調整弁と前記排気弁を制御する制御装置と、を備え、
前記制御装置は、前記洗濯槽を密閉した状態で前記給水弁を開くことで水道の供給圧力によって水道水を前記洗濯槽内に導入し、かつ、前記給水圧力調整弁と前記排気弁を制御して水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように前記洗濯槽内の水に前記洗濯槽内のガスを溶解させることを特徴とする洗濯機。
A washing machine with a sealable washing tub,
A water supply pipe that is connected to the water supply pipe and supplies the tap water flowing through the water supply pipe to the washing tub, a water supply valve that opens and closes the flow path of the water supply pipe, and is supplied into the washing tub through the water supply pipe. A water supply pressure adjusting valve for adjusting the pressure of the tap water, an exhaust pipe for exhausting the gas in the washing tub, an exhaust valve for opening and closing a flow path of the exhaust pipe, the water supply valve, and the water supply pressure adjusting valve, A control device for controlling the exhaust valve,
The control device introduces tap water into the washing tub by water supply pressure by opening the water supply valve in a state where the washing tub is sealed, and controls the water supply pressure adjusting valve and the exhaust valve. The washing machine is characterized in that the gas in the washing tub is dissolved in the water in the washing tub so that the total dissolved gas concentration in water is 120% or more of the saturation solubility under atmospheric pressure.
前記制御装置は、前記洗濯槽を密閉した状態で前記給水弁を開くことで水道の供給圧力によって水道水を前記洗濯槽内に導入し、かつ、前記給水圧力調整弁と前記排気弁を制御して水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように前記洗濯槽内の水に前記洗濯槽内のガスを溶解させた後、前記給水弁を閉じ、かつ前記排気弁を開いて前記洗濯槽内を大気圧に開放することにより、当該洗濯槽内の水において過飽和となった溶存ガスを微細気泡として発生させることを特徴とする請求項1に記載の洗濯機。   The control device introduces tap water into the washing tub by water supply pressure by opening the water supply valve in a state where the washing tub is sealed, and controls the water supply pressure adjusting valve and the exhaust valve. After dissolving the gas in the washing tub in the water in the washing tub so that the total dissolved gas concentration in water is 120% or more of the saturation solubility under atmospheric pressure, the water supply valve is closed, and the exhaust The washing machine according to claim 1, wherein a dissolved gas that is supersaturated in water in the washing tub is generated as fine bubbles by opening a valve to open the washing tub to atmospheric pressure. 前記洗濯槽内の圧力を減圧する減圧手段をさらに備え、
前記制御装置は、前記洗濯槽内を大気圧に開放した後、さらに前記減圧手段で前記洗濯槽内を大気圧以下に減圧することにより、前記微細気泡の発生を促進させることを特徴とする請求項2に記載の洗濯機。
A pressure reducing means for reducing the pressure in the washing tub;
The said control apparatus accelerates | stimulates generation | occurrence | production of the said fine bubble by decompressing the inside of the said washing tub to below atmospheric pressure with the said pressure reduction means, after opening the inside of the said washing tub to atmospheric pressure. Item 3. A washing machine according to Item 2.
前記制御装置は前記減圧手段で前記洗濯槽内を減圧して、該洗濯槽内の水中の溶存ガス濃度を大気圧下の飽和溶解度の80%以下にすることを特徴とする請求項3に記載の洗濯機。   The said control apparatus decompresses the inside of the said washing tub with the said pressure reduction means, The dissolved gas density | concentration in the water in this washing tub is made into 80% or less of the saturation solubility under atmospheric pressure, It is characterized by the above-mentioned. Washing machine. 前記水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように前記洗濯槽内の水に前記洗濯槽内のガスを溶解させるとき、前記洗濯槽を回転又は揺動させて、前記洗濯槽内に導入された水道水に対して乱流を形成する機構をさらに備えたことを特徴とする請求項1から4のいずれか1項に記載の洗濯機。   When the gas in the washing tub is dissolved in the water in the washing tub so that the total dissolved gas concentration in the water is 120% or more of the saturation solubility under atmospheric pressure, the washing tub is rotated or swung. The washing machine according to any one of claims 1 to 4, further comprising a mechanism for forming a turbulent flow with respect to the tap water introduced into the washing tub. 前記洗濯槽内に導入する水道水を、硬度50mgCaCO3/l以下の軟水とする軟水化装置をさらに備えたことを特徴とする請求項1から5のいずれか1項に記載の洗濯機。 The washing machine according to any one of claims 1 to 5, further comprising a water softening device that converts tap water introduced into the washing tub into soft water having a hardness of 50 mg CaCO 3 / l or less. 前記洗濯槽内に導入する水道水を、導電率100μS/cm以下、より好ましくは導電率50μS/cm以下の脱塩水とする脱塩装置をさらに備えたことを特徴とする請求項1から5のいずれか1項に記載の洗濯機。   The demineralizer which makes the tap water introduce | transduced in the said washing tub into the demineralized water of electrical conductivity 100microS / cm or less, More preferably, electrical conductivity 50microS / cm or less is further provided. The washing machine according to any one of claims. 水道水を用いて洗濯槽内の洗濯物を洗う洗濯方法であって、
前記洗濯槽内に洗濯物を投入した後、前記洗濯槽を密閉した状態で水道の供給圧力によって水道水を前記洗濯槽内に導入し、かつ、該洗濯槽への水道水の導入圧と該洗濯槽内の圧力を制御して水中の全溶存ガス濃度が大気圧下の飽和溶解度の120%以上となるように前記洗濯槽内の水に前記洗濯槽内のガスを溶解させることを特徴とする洗濯方法。
A washing method for washing laundry in a washing tub using tap water,
After the laundry is put into the washing tub, tap water is introduced into the washing tub by a water supply pressure in a state where the washing tub is sealed, and the tap water introduction pressure into the washing tub and the The pressure in the washing tub is controlled to dissolve the gas in the washing tub in the water in the washing tub so that the total dissolved gas concentration in the water becomes 120% or more of the saturation solubility under atmospheric pressure. How to wash.
前記洗濯槽内の水に前記洗濯槽内のガスを溶解させた後、前記洗濯槽内を大気圧に開放することにより、当該洗濯槽内の水において過飽和となった溶存ガスを前記洗濯物の繊維内部、あるいは洗濯物表面で微細気泡として発生させ、該微細気泡によって汚れを浮き上がらせて除去することを特徴とする請求項8に記載の洗濯方法。   After the gas in the washing tub is dissolved in the water in the washing tub, the dissolved gas that has become supersaturated in the water in the washing tub is released by releasing the inside of the washing tub to atmospheric pressure. The washing method according to claim 8, wherein fine bubbles are generated inside the fiber or on the surface of the laundry, and dirt is lifted and removed by the fine bubbles. 前記洗濯槽内を大気圧に開放した後、さらに当該洗濯槽内を大気圧以下に減圧することにより、前記微細気泡の発生を促進させてより強力な汚れ除去効果を得ることを特徴とする請求項9に記載の洗濯方法。   After releasing the inside of the washing tub to atmospheric pressure, the inside of the washing tub is further reduced to the atmospheric pressure or less, thereby promoting the generation of the fine bubbles and obtaining a stronger dirt removing effect. Item 10. The washing method according to Item 9. 前記洗濯槽内を減圧して、該洗濯槽内の水中の溶存ガス濃度を大気圧下の飽和溶解度の80%以下にすることを特徴とする請求項10に記載の洗濯方法。   The washing method according to claim 10, wherein the inside of the washing tub is decompressed so that the dissolved gas concentration in the water in the washing tub is 80% or less of the saturated solubility under atmospheric pressure. 洗剤使用量を標準使用量の1/3以下とすることを特徴とする請求項8から11のいずれか1項に記載の洗濯方法。   The washing method according to any one of claims 8 to 11, wherein the amount of detergent used is 1/3 or less of the standard amount of use. 前記洗濯槽内に導入する水道水を、硬度50mgCaCO3/l以下の軟水とすることを特徴とする請求項8から12のいずれか1項に記載の洗濯方法。 The washing method according to any one of claims 8 to 12, wherein the tap water introduced into the washing tub is soft water having a hardness of 50 mg CaCO 3 / l or less. 前記洗濯槽内に導入する水道水を、導電率100μS/cm以下、より好ましくは導電率50μS/cm以下の脱塩水とすることを特徴とする請求項8から12のいずれか1項に記載の洗濯方法。   13. The tap water introduced into the washing tub is demineralized water having a conductivity of 100 μS / cm or less, more preferably a conductivity of 50 μS / cm or less. How to wash.
JP2012216885A 2012-09-28 2012-09-28 Washing machine, and washing method Pending JP2014068798A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101848668B1 (en) * 2016-11-17 2018-04-13 엘지전자 주식회사 Laundry Treating Apparatus
CN109989219A (en) * 2017-12-29 2019-07-09 青岛海尔滚筒洗衣机有限公司 A kind of control method and laundry drying clothes integrated machine of drying clothes integrated machine of doing washing
TWI666357B (en) * 2015-12-25 2019-07-21 日商東芝生活電器股份有限公司 washing machine
CN112342732A (en) * 2019-07-22 2021-02-09 无锡飞翎电子有限公司 Washing machine water inlet control method and device, washing machine and storage medium

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI666357B (en) * 2015-12-25 2019-07-21 日商東芝生活電器股份有限公司 washing machine
KR101848668B1 (en) * 2016-11-17 2018-04-13 엘지전자 주식회사 Laundry Treating Apparatus
CN109989219A (en) * 2017-12-29 2019-07-09 青岛海尔滚筒洗衣机有限公司 A kind of control method and laundry drying clothes integrated machine of drying clothes integrated machine of doing washing
CN109989219B (en) * 2017-12-29 2022-09-16 重庆海尔滚筒洗衣机有限公司 Control method of washing and drying integrated machine and washing and drying integrated machine
CN112342732A (en) * 2019-07-22 2021-02-09 无锡飞翎电子有限公司 Washing machine water inlet control method and device, washing machine and storage medium
CN112342732B (en) * 2019-07-22 2023-08-15 无锡飞翎电子有限公司 Washing machine water inlet control method and device, washing machine and storage medium

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