JP4516704B2 - Superheated steam drying method and apparatus - Google Patents

Superheated steam drying method and apparatus Download PDF

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Publication number
JP4516704B2
JP4516704B2 JP2001156303A JP2001156303A JP4516704B2 JP 4516704 B2 JP4516704 B2 JP 4516704B2 JP 2001156303 A JP2001156303 A JP 2001156303A JP 2001156303 A JP2001156303 A JP 2001156303A JP 4516704 B2 JP4516704 B2 JP 4516704B2
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Prior art keywords
drying
circulation duct
dried
superheated steam
steam
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JP2002346295A (en
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敏夫 服部
宏幸 朝岡
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Inamoto Manufacturing Co Ltd
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Inamoto Manufacturing Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、衣料やタオル等の布地を乾燥させる過熱蒸気式乾燥方法及びその装置に関する。
【0002】
【従来の技術】
従来の乾燥機は、図3に示すように、外部からの新鮮な空気を送風ファン31で取り込み、これを加熱ヒータ32により加熱して乾燥ドラム33へ送る。乾燥ドラム33では、水分を含んだ衣料や、リネン、タオル等の被乾燥物20を攪拌しながら、上記加熱された空気に接触することによって乾燥する。衣料等を乾燥させた空気は、排気ダクト34を介して、糸屑除去フィルタ35を通り、屋外へと排出される。図3は、送風ファン31を乾燥ドラム33に対して空気が流入する入口側に設けており、押し込み型と一般に言われている。一方、図4は、送風ファン31を乾燥ドラム33に対して出口側に設けており、吸い込み型と一般に言われている。この押し込み型も吸い込み型も、外部からの新鮮な空気を加熱して、被乾燥物20に接触させた後、屋外に排気するという熱風の供給方法であり、現在、多くの乾燥機で採用している。
【0003】
しかし、このように加熱した新鮮な空気を乾燥ドラム33通過後は屋外に排出してしまうという一方通行的な熱風の供給方法では、被乾燥物20との接触効率が低いため、加熱された空気が被乾燥物20に接触しないまま排気ダクト34を介して屋外へ排出される場合があり、熱ロスが大きいのが欠点である。このような一方通行的な供給方法では、実際に空気を加熱した熱量が、被乾燥物20内の水分を乾燥させるために必要な熱量の約2倍にもなったという報告もある。したがって、熱効率を向上させ、省エネルギーで被乾燥物を乾燥する方法の開発が望まれている。
また、このような一方通行的な供給方法は、大口径の排気ダクトを設置する必要があるため、装置自体が大きくなると伴に、装置を設置するコストも高いという問題がある。さらに、排ガスを屋外に放出するため、異臭も屋外に排出してしまうという問題もある。
このような状況に鑑みて、特開昭61−73699号公報にあるようなドライな過熱蒸気を用いてぬれた布地を乾燥させるための方法が記載されているが、この方法では布地を出し入れする度に乾燥内の蒸気が外に出てしまい効率が悪い。
【0004】
【発明が解決しようとする課題】
本発明は、熱効率を向上させて省エネルギー化を図ることが可能で、排気ダクトを採用しないため異臭を屋外に排出しないドラム式乾燥方法及びその装置を提供することを目的とする。
【0005】
【課題を解決するための手段】
本発明に係る過熱蒸気式乾燥方法は、被乾燥物である水分を含んだ布地を過熱蒸気を利用して乾燥させるドラム式乾燥機において、乾燥ドラムと循環ダクトとを含んでなる主構成経路に蒸気を供給しつつ、該主構成経路内に初期からあった空気を該主構成経路外の空気貯留手段に導き、該主構成経路を閉回路にした後、該主構成経路内で過熱蒸気を循環させることによって該被乾燥物の水分を蒸発させることを特徴とする。
上記過熱蒸気としては、100℃〜150℃の温度範囲の過熱蒸気を用いることができる。
また、上記被乾燥物の水分が蒸発することによって該主構成経路内の圧力が上昇するが、その内圧の上昇分のみの蒸気を冷却して凝縮水として回収し、排ガスを屋外に放出しないようにすることができる。
【0006】
このような構成により、過熱蒸気が循環して被乾燥物に接触するため、被乾燥物に接触しないまま屋外に排出されるという熱ロスはほぼ零となり、熱効率が大幅に向上し、省エネルギー化することができる。また、被乾燥物から蒸発される水分は、排気ダクトを採用せずに凝縮水として回収するため、異臭の屋外排気を防ぐことができる。さらに、100℃以上の温度で乾燥し、乾燥終了時点では被乾燥物自体の温度も100℃以上になるため、病院等のリネン類の乾燥にも用い得る十分な殺菌効果を有することができる。
【0007】
また、本発明に係る過熱蒸気式乾燥装置は、被乾燥物である水分を含んだ布地を攪拌する乾燥ドラムと、該乾燥ドラムの出口と入口をつなぐ循環ダクトと、該循環ダクトに設置された循環ファン及び過熱ヒータと、該循環ダクトに接続された蒸気供給管と、該循環ダクトの一部分を迂回するように該循環ダクトの一位置と他の位置を結ぶバイパス管と、該バイパス管に設けられた該乾燥ドラム及び該循環ダクト内の空気を保留するためのエアバッグのような空気貯留手段と、該バイパス管又は該循環ダクトに設けられた冷却用のコンデンサとを含んでなり、該乾燥ドラムと該循環ダクトとを含んでなる主構成経路が閉回路であることを特徴とする。
上記過熱蒸気式乾燥装置はドラム式洗濯乾燥装置に用いることができる。
【0008】
【発明の実施の形態】
添付図面に基づいて、本発明の実施の形態を詳細に説明する。
図1は、本発明の一実施の形態であって、過熱蒸気式乾燥装置の概略を示す構成図である。図1に示すように、本発明に係る過熱蒸気式乾燥装置は、水分を含んだ衣料や、リネン、タオル等といった被乾燥物20をタンブリング(攪拌)させる乾燥ドラム1を備えており、また、この乾燥ドラム1は、被乾燥物20をドラム1内に投入するためのドア2を正面に備えている。乾燥ドラム1は、空気や蒸気を通気させるために、その外周面に孔が開いている。また、乾燥ドラム1は、洗濯と乾燥の併用機の場合、洗濯ドラムとしても用いることができる。ドア2は乾燥ドラム1内を密封状態にできるように、外周縁にシールを取り付けている。
【0009】
また、乾燥ドラム1の出口と入口は循環ダクト3でつながれており、この乾燥ドラム1と循環ダクト3とを本発明では主構成経路という。乾燥ドラム1の出口は、図1に示すように、乾燥ドラム1の上方部に設けられているが、下方部に設けることもできる。乾燥のみの単体機の場合、蒸気が被乾燥物20からの蒸発水分を含み比重が重くなるため、出口を下方部に設けるのが好ましい。一方、洗濯と乾燥の兼用機の場合、下方部は洗濯排水等の設備があるため、出口を上方部に設けるのが好ましい。乾燥ドラム1の入口は、乾燥ドラム1の上方部にあっても下方部にあっても良い。
【0010】
循環ダクト3は、主構成経路内に循環流を作るための循環ファン4と、主構成経路内の循環蒸気を過熱蒸気に過熱するための過熱ヒータ5と、主構成経路内に水蒸気を供給するための蒸気供給管6とを備えている。
循環ファン4は、循環ダクト3内のどの位置に設置しても良いが、乾燥ドラム1内の空気や蒸気を循環ダクト3内に効率良く吸い込むため、乾燥ドラム1の出口付近に設置するのが好ましい。また、循環ファン4は、電動式モータ等によって駆動させる。
過熱ヒータ5は、循環ダクト3内のどの位置に設置しても良いが、過熱した水蒸気を熱ロスが少ないように乾燥ドラム1内に供給するため、乾燥ドラム1の入口付近に設置するのが好ましい。また、過熱ヒータ5は、蒸気を温度100℃〜150℃まで上昇させることができる性能のもので十分である。
蒸気供給管6は、循環ダクト3内のどの位置に設置しても良いが、水蒸気を供給することによって主構成経路内の初期にあった空気を逆止弁11から、空気の一時保留手段であるエアバッグ14に追い出すため、乾燥ドラム1を挟んで逆止弁11の反対側に設置するのが好ましい。また、蒸気供給管6は、循環ダクト3と接続する位置付近に蒸気供給弁7を備えており、他方は、図に示されていないが蒸気供給源につながっている。
【0011】
循環ダクト3の一部を迂回するように、循環ダクト3の一位置と他の位置の二点はバイパス管10でつながれている。その循環ダクト3とバイパス管10とをつなぐ2点の位置は、特に限定されないが、1点は主構成経路内の初期空気を逆止弁11から追い出すため、乾燥ドラム1と循環ファン4の間のいずれかの位置が好ましく、もう1点は乾燥終了後に主構成経路に空気を効率良く送り込むため、循環ファン4と過熱ヒータ5の間のいずれかの最頂部(頂点)位置が好ましい。
バイパス管10は、上流側から順に、圧力により弁を開閉するための逆止弁11と、蒸気を冷却して凝縮するためのコンデンサ12と、自動的に弁を開閉するための自動弁A13と、主構成経路内にある空気を一時的に保留するためのエアバッグ14と、エアバッグ14内に保留していた空気を再び主構成経路内に送り出すための送気ブロア15と、自動的に弁を開閉するための自動弁B16とを備えている。
【0012】
逆止弁11は、コンデンサ12やバイパス14から主構成経路への蒸気の逆流を防止するように弁体が作動する弁であれば、特に限定されず、例えば、リフト逆止弁、スイング逆止弁、ボール逆止弁を用いることができる。また、逆止弁11の代わりに、例えば、細い管を循環ダクト3とコンデンサ12の間に設けることもできるし、循環ダクト3内に設けた湿度計の値により開閉する弁を設けることもできる。
エアバッグ14は、主構成経路内に初期からある空気を一時的に保留できる容積が必要であり、乾燥ドラム1の大きさによって適宜その大きさを設計することができる。例えば、0.5m3程度とすることができる。樹脂製容器又は伸縮性のある樹脂製バック等を用いることができる。
【0013】
このような構成によれば、乾燥単体機の場合、別置の洗濯専用機から洗濯済みの水分を含んだ被乾燥物20を乾燥ドラム1に投入してドア2を閉めた後、又は洗濯乾燥兼用機の場合、洗濯工程が終了した後、循環ファン4と過熱ヒータ5を起動すると伴に、蒸気供給弁7を開いて蒸気供給管6から蒸気を主構成経路内に供給する。この時、自動弁A13は開き、自動弁B16は閉じ、送風ブロア15は停止している。蒸気が供給されると、主構成経路内に初期からあった空気は、逆止弁11からバイパス管10に追い出される。コンデンサ12で空気中の水分が冷却されて凝縮されるが、その他の空気は、自動弁A13を介してエアバッグ14まで追い出され、ここで一時的に保留される。
【0014】
主構成経路内の初期空気をエアバッグ14に保留するのが完了した後、蒸気供給弁7を閉じて水蒸気の供給を止めると伴に、自動弁A13も閉じる。これにより、主構成経路内は空気が除去された閉回路となる。温度が約100℃である主構成経路内の循環蒸気を、過熱ヒータ5により100℃〜150℃の温度範囲まで、好ましくは120〜130℃まで上昇して過熱蒸気化する。過熱蒸気が100℃近辺の場合、被乾燥物20に含まれる水分を蒸発させるのに時間がかかるため、好ましくない。過熱蒸気の温度は120℃以上が一般的に効率が良い。一方、150℃を超える場合、被乾燥物20が熱のため変色したりするので、注意を要し、好ましくない。
【0015】
この過熱蒸気によって温度乾燥ドラム1内の被乾燥物20に含まれる水分が蒸発し、被乾燥物20は乾燥する。被乾燥物20内の水分の蒸発が盛んに始まると、主構成経路内ではその蒸発水分に匹敵する内圧上昇が起こる。この内圧上昇分が逆止弁11を開き、蒸発水分を含んだ蒸気がバイパス管10を経てコンデンサ12に導入される。コンデンサ12は蒸気を冷却して凝縮(液化)し、図に示していないが回収容器等へ凝縮水を排出する。
【0016】
被乾燥物20の乾燥を終えた後、循環ファン4と過熱ヒータ5の運転を止める。そして、自動弁B16を開き、送気ブロア15を起動することにより、エアバッグ14内に一時保留していた空気を再び主構成経路へ供給する。この時、自動弁A13は閉じたままである。したがって、主構成経路内に残留している蒸気は、逆止弁を通り、バイパス管10を経て、コンデンサ12へ導入される。コンデンサ12は、乾燥中と同様に、蒸気を冷却して凝縮し、凝縮水として排出する。
空気の再供給が完了した後、自動弁B16を閉じる。そして、ドア2を開き、乾燥ドラム1内の乾燥した被乾燥物20を取り出す。
【0017】
ここで、図2に示すように、逆止弁11の代わりに、細い管を循環ダクト3とコンデンサ12の間に設けることもできる。これにより、内圧の上昇を待たずに、積極的に主構成経路内の蒸発水分をコンデンサ12により冷却して除去することができるので、逆止弁11を設けた場合に比べて、被乾燥物20の乾燥を速く行うことができる。但し、内圧上昇分以上の冷却を行うため、逆止弁11を設けた場合に比べて、過熱ヒータ5でより過熱する必要があり、熱効率は悪くなる。
また、上記細管の入口には、循環ダクト3内に設けた湿度計の値により開閉する弁を設けることもできる。これにより、内圧の上昇を待たずに、湿度調整により主構成経路内の蒸発水分をコンデンサ12により冷却して除去することができるので、被乾燥物20の乾燥を速く行うことができる。但し、内圧上昇分以上の冷却を行うため、上記と同様に、過熱ヒータ5でより過熱する必要があり、熱効率は悪くなる。
さらに、コンデンサ12はバイパス管10に設けられているが、循環ダクト3に設けることもできる。これにより、主構成経路内の蒸発水分を冷却して除去することができるので、バイパス管10に設けた場合に比べて、被乾燥物20の乾燥を速く行うことができる。但し、主構成経路内で冷却を行うため、バイパス管10に設けた場合に比べて、過熱ヒータ5でより過熱する必要があり、熱効率は悪くなる。
【0018】
【発明の効果】
上記説明したように、本発明は、主構成経路が閉回路を構成することにより、過熱蒸気が循環して被乾燥物に接触するため、被乾燥物に接触しないまま屋外へ排出されるという熱ロスはほぼ零となる。主構成経路外への熱放出は、被乾燥物からの水分蒸発による内圧上昇分のみとなり、したがって、被乾燥物の乾燥に必要な熱量は、装置の放熱によるロスが若干あるが、ほぼ残留水分の蒸発のみとなり、従来の一方通行的な熱風の供給方法に比べて熱効率が大幅に向上し、従来比で40〜50%の省エネルギーが可能となる。
【0019】
また、本発明は、主構成経路内の初期空気をエアバッグに一時貯留することにより、屋外への排気を不要にすることができる。また、被乾燥物からの蒸発水分をコンデンサにより冷却して凝縮水として回収するため、異臭成分を凝縮水に取り込むことができる。したがって、屋外への排気を実質的に不要にすることができ、異臭の屋内外への流出を防ぐことができる。また、主構成経路内の初期空気を排除するため、被乾燥物が乾燥時に酸素により酸化されず、衣類等にやさしい乾燥をすることができる。
【0020】
したがって、本発明によれば、熱効率を向上させて省エネルギー化することが可能で、排気ダクトを採用しないため異臭を屋外に排出しない過熱蒸気式乾燥方法及びその装置を提供することができる。
【図面の簡単な説明】
【図1】本発明に係る過熱蒸気式乾燥装置の概略を示す構成図である。
【図2】本発明に係る過熱蒸気式乾燥装置の一代替例を示す構成図である。
【図3】従来の押し込み型のドラム式乾燥装置の概略を示す構成図である。
【図4】従来の吸い込み型のドラム式乾燥装置の概略を示す構成図である。
【符号の説明】
1 乾燥ドラム
2 ドア
3 循環ダクト
4 循環ファン
5 過熱ヒータ
6 蒸気供給管
7 蒸気供給弁
10 バイパス管
11 逆止弁
12 コンデンサ
13 自動弁A
14 エアバッグ
15 送気ブロア
16 自動弁B
20 被乾燥物
31 送気ファン
32 加熱ヒータ
33 乾燥ドラム
34 排気ダクト
35 糸屑除去フィルタ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a superheated steam drying method and apparatus for drying cloth such as clothing and towels.
[0002]
[Prior art]
As shown in FIG. 3, the conventional dryer takes in fresh air from the outside with a blower fan 31, heats it with a heater 32, and sends it to a drying drum 33. The drying drum 33 dries by contacting the heated air while stirring the clothes 20 containing moisture, the linen, the towel, and the like. The air that has dried clothes and the like passes through the exhaust duct 34, passes through the lint removal filter 35, and is discharged outside. In FIG. 3, the blower fan 31 is provided on the inlet side where air flows into the drying drum 33, and is generally called a push-in type. On the other hand, in FIG. 4, the blower fan 31 is provided on the outlet side with respect to the drying drum 33 and is generally called a suction type. Both the push-in type and the suction type are hot air supply methods in which fresh air from the outside is heated and brought into contact with the object to be dried 20 and then exhausted to the outside. Currently, it is used in many dryers. ing.
[0003]
However, in the one-way hot air supply method in which fresh air heated in this way is discharged to the outside after passing through the drying drum 33, the contact efficiency with the object to be dried 20 is low, and thus the heated air May be discharged to the outside through the exhaust duct 34 without being in contact with the object to be dried 20, and the disadvantage is that the heat loss is large. In such a one-way supply method, there is a report that the amount of heat actually heated by the air is about twice as much as the amount of heat necessary for drying the moisture in the object to be dried 20. Therefore, development of a method for improving the thermal efficiency and drying an object to be dried with energy saving is desired.
In addition, such a one-way supply method requires the installation of a large-diameter exhaust duct, so that there is a problem that the cost of installing the device is high as the device itself becomes large. Furthermore, since the exhaust gas is released outdoors, there is also a problem that off-flavors are also emitted outdoors.
In view of such circumstances, a method for drying wet fabric using dry superheated steam as described in JP-A-61-73699 has been described. In this method, fabric is taken in and out. Each time the steam in the drying comes out, the efficiency is poor.
[0004]
[Problems to be solved by the invention]
SUMMARY OF THE INVENTION An object of the present invention is to provide a drum-type drying method and an apparatus thereof that can improve energy efficiency and save energy, and do not discharge an odor to the outdoors because an exhaust duct is not employed.
[0005]
[Means for Solving the Problems]
The superheated steam type drying method according to the present invention is a drum-type dryer that uses a superheated steam to dry a moisture-containing fabric, which is an object to be dried, in a main constituent path including a drying drum and a circulation duct. While supplying steam, the air from the beginning in the main component path is guided to the air storing means outside the main component path, and the main component path is closed circuit, and then superheated steam is generated in the main component path. It is characterized by evaporating the moisture of the material to be dried by circulation.
As the superheated steam, superheated steam having a temperature range of 100 ° C to 150 ° C can be used.
Also, the moisture in the material to be dried evaporates to increase the pressure in the main component path, but the steam corresponding to the increase in the internal pressure is cooled and collected as condensed water, and the exhaust gas is not released outdoors. Can be.
[0006]
With such a configuration, since the superheated steam circulates and contacts the object to be dried, the heat loss of being discharged outside without contacting the object to be dried becomes substantially zero, greatly improving the thermal efficiency and saving energy. be able to. Moreover, since the water | vapor evaporated from a to-be-dried object is collect | recovered as condensed water, without employ | adopting an exhaust duct, it can prevent the off-air exhaust with a strange odor. Furthermore, since drying is performed at a temperature of 100 ° C. or higher and the temperature of the object to be dried itself is 100 ° C. or higher at the end of drying, it can have a sufficient sterilizing effect that can be used for drying hospital linens and the like.
[0007]
Further, the superheated steam drying apparatus according to the present invention is installed in a drying drum that stirs a fabric containing moisture, which is an object to be dried, a circulation duct that connects an outlet and an inlet of the drying drum, and the circulation duct. A circulation fan and a superheater; a steam supply pipe connected to the circulation duct; a bypass pipe connecting one position of the circulation duct to another position so as to bypass a part of the circulation duct; and provided in the bypass pipe Air drying means such as an air bag for retaining the air in the drying drum and the circulation duct, and a cooling condenser provided in the bypass pipe or the circulation duct. The main constituent path including the drum and the circulation duct is a closed circuit.
The superheated steam dryer can be used in a drum-type laundry dryer.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 is a block diagram showing an outline of a superheated steam dryer according to an embodiment of the present invention. As shown in FIG. 1, the superheated steam type drying apparatus according to the present invention includes a drying drum 1 for tumbling (stirring) an object to be dried 20 such as clothes containing moisture, linen, towels, etc. The drying drum 1 is provided with a door 2 on the front side for feeding an object to be dried 20 into the drum 1. The drying drum 1 has a hole in its outer peripheral surface to allow air and steam to pass through. The drying drum 1 can also be used as a washing drum in the case of a combined washing and drying machine. The door 2 has a seal attached to the outer periphery so that the inside of the drying drum 1 can be sealed.
[0009]
Further, the outlet and the inlet of the drying drum 1 are connected by a circulation duct 3, and the drying drum 1 and the circulation duct 3 are referred to as a main constituent path in the present invention. As shown in FIG. 1, the outlet of the drying drum 1 is provided in the upper part of the drying drum 1, but can also be provided in the lower part. In the case of a single machine only for drying, it is preferable to provide an outlet at the lower part because the steam contains evaporated water from the material to be dried 20 and the specific gravity becomes heavy. On the other hand, in the case of a combined washing and drying machine, since the lower part has facilities such as washing drainage, the outlet is preferably provided in the upper part. The inlet of the drying drum 1 may be in the upper part or the lower part of the drying drum 1.
[0010]
The circulation duct 3 supplies a circulation fan 4 for creating a circulation flow in the main component path, a superheater 5 for heating the circulation steam in the main component path to superheated steam, and steam in the main component path. And a steam supply pipe 6 for the purpose.
The circulation fan 4 may be installed at any position in the circulation duct 3. However, in order to efficiently suck the air and steam in the drying drum 1 into the circulation duct 3, the circulation fan 4 is installed in the vicinity of the outlet of the drying drum 1. preferable. The circulation fan 4 is driven by an electric motor or the like.
The superheater 5 may be installed at any position in the circulation duct 3. However, in order to supply the superheated water vapor into the drying drum 1 so as to reduce heat loss, the superheater 5 is installed near the inlet of the drying drum 1. preferable. Moreover, the thing of the performance which can raise a vapor | steam to the temperature of 100 to 150 degreeC is enough for the superheater 5.
The steam supply pipe 6 may be installed at any position in the circulation duct 3, but by supplying water vapor, the air that was initially in the main component path is removed from the check valve 11 by air temporarily storing means. In order to expel it to a certain airbag 14, it is preferable to install it on the opposite side of the check valve 11 with the drying drum 1 in between. Further, the steam supply pipe 6 is provided with a steam supply valve 7 in the vicinity of a position where it is connected to the circulation duct 3, and the other is connected to a steam supply source (not shown).
[0011]
Two points of one position of the circulation duct 3 and another position are connected by a bypass pipe 10 so as to bypass a part of the circulation duct 3. The position of the two points connecting the circulation duct 3 and the bypass pipe 10 is not particularly limited, but one point drives out the initial air in the main component path from the check valve 11, so that there is a gap between the drying drum 1 and the circulation fan 4. The other point is preferable, and the other point is preferably the top (vertical) position between the circulation fan 4 and the superheater heater 5 in order to efficiently send air to the main constituent path after completion of drying.
The bypass pipe 10 includes, in order from the upstream side, a check valve 11 for opening and closing the valve by pressure, a condenser 12 for cooling and condensing steam, and an automatic valve A13 for automatically opening and closing the valve. An air bag 14 for temporarily holding the air in the main component path, an air supply blower 15 for sending the air held in the airbag 14 again into the main component path, and automatically And an automatic valve B16 for opening and closing the valve.
[0012]
The check valve 11 is not particularly limited as long as the valve body operates so as to prevent the backflow of steam from the condenser 12 or the bypass 14 to the main component path. For example, the check valve 11 is a lift check valve or a swing check valve. A valve or a ball check valve can be used. Further, instead of the check valve 11, for example, a thin tube can be provided between the circulation duct 3 and the condenser 12, or a valve that opens and closes depending on the value of a hygrometer provided in the circulation duct 3 can be provided. .
The air bag 14 needs a volume capable of temporarily retaining air from the beginning in the main component path, and the size can be appropriately designed according to the size of the drying drum 1. For example, it can be set to about 0.5 m 3 . A resin container or a stretchable resin bag can be used.
[0013]
According to such a configuration, in the case of a single drying machine, after an object to be dried 20 containing water that has been washed is put into the drying drum 1 from the separate washing machine and the door 2 is closed, or after washing and drying. In the case of the dual-purpose machine, after the washing process is completed, the circulation fan 4 and the superheater heater 5 are started, and the steam supply valve 7 is opened to supply steam from the steam supply pipe 6 into the main component path. At this time, the automatic valve A13 is opened, the automatic valve B16 is closed, and the blower blower 15 is stopped. When steam is supplied, the air that was originally in the main component path is expelled from the check valve 11 to the bypass pipe 10. Water in the air is cooled and condensed by the condenser 12, but the other air is expelled to the airbag 14 via the automatic valve A13 and temporarily held there.
[0014]
After the initial air in the main component path is held in the airbag 14, the steam supply valve 7 is closed to stop the supply of water vapor, and the automatic valve A13 is also closed. Thereby, the inside of the main component path is a closed circuit from which air is removed. The circulating steam in the main constituent path having a temperature of about 100 ° C. is heated to a temperature range of 100 ° C. to 150 ° C., preferably 120 to 130 ° C., and superheated by the superheater 5. When the superheated steam is near 100 ° C., it takes time to evaporate the moisture contained in the material 20 to be dried, which is not preferable. In general, the temperature of the superheated steam is 120 ° C. or higher. On the other hand, if the temperature exceeds 150 ° C., the object to be dried 20 may be discolored due to heat, which requires attention and is not preferable.
[0015]
The moisture contained in the material to be dried 20 in the temperature drying drum 1 is evaporated by this superheated steam, and the material to be dried 20 is dried. When the evaporation of moisture in the object to be dried 20 starts vigorously, an internal pressure rise comparable to the evaporated moisture occurs in the main constituent path. This increase in internal pressure opens the check valve 11, and steam containing evaporated water is introduced into the condenser 12 through the bypass pipe 10. The condenser 12 cools and condenses (liquefies) the steam, and discharges condensed water to a collection container or the like (not shown).
[0016]
After drying the object to be dried 20, the operation of the circulation fan 4 and the superheater heater 5 is stopped. Then, by opening the automatic valve B16 and starting the air supply blower 15, the air temporarily held in the airbag 14 is supplied again to the main component path. At this time, the automatic valve A13 remains closed. Therefore, the steam remaining in the main component path passes through the check valve and is introduced into the condenser 12 through the bypass pipe 10. The condenser 12 cools and condenses the steam as in the drying process, and discharges it as condensed water.
After the resupply of air is completed, the automatic valve B16 is closed. Then, the door 2 is opened and the dried material 20 to be dried in the drying drum 1 is taken out.
[0017]
Here, as shown in FIG. 2, a thin tube may be provided between the circulation duct 3 and the condenser 12 instead of the check valve 11. Thus, the evaporated water in the main component path can be positively cooled and removed by the condenser 12 without waiting for the internal pressure to rise, so that the object to be dried is more than that when the check valve 11 is provided. 20 can be dried quickly. However, in order to cool more than the increase in internal pressure, it is necessary to overheat with the superheater 5 as compared with the case where the check valve 11 is provided, and the thermal efficiency is deteriorated.
A valve that opens and closes according to the value of a hygrometer provided in the circulation duct 3 can be provided at the inlet of the thin tube. Thereby, the evaporating water in the main component path can be cooled and removed by the capacitor 12 by adjusting the humidity without waiting for the internal pressure to rise, so that the object to be dried 20 can be quickly dried. However, in order to perform cooling that is equal to or greater than the increase in internal pressure, it is necessary to further heat with the superheater 5 as described above, resulting in poor thermal efficiency.
Furthermore, although the capacitor 12 is provided in the bypass pipe 10, it can also be provided in the circulation duct 3. As a result, the evaporated water in the main configuration path can be cooled and removed, so that the object to be dried 20 can be dried faster than the case where it is provided in the bypass pipe 10. However, since cooling is performed in the main configuration path, it is necessary to heat the superheater 5 more than in the case where the bypass pipe 10 is provided, and the thermal efficiency is deteriorated.
[0018]
【The invention's effect】
As described above, according to the present invention, since the main configuration path forms a closed circuit, the superheated steam circulates and comes into contact with the object to be dried, so that the heat is discharged outside without contacting the object to be dried. Loss is almost zero. Heat release to the outside of the main component path is only the increase in internal pressure due to moisture evaporation from the object to be dried.Therefore, the amount of heat required for drying the object to be dried is slightly reduced due to heat dissipation of the device, but almost no residual moisture. As compared with the conventional one-way hot air supply method, the thermal efficiency is greatly improved, and 40-50% of energy can be saved compared to the conventional one.
[0019]
In addition, according to the present invention, it is possible to eliminate the need for exhaust to the outdoors by temporarily storing the initial air in the main component path in the airbag. Further, since the evaporated water from the object to be dried is cooled by the condenser and collected as condensed water, the off-flavor component can be taken into the condensed water. Therefore, it is possible to substantially eliminate the need for exhaust to the outdoors, and to prevent the outflow of a strange odor to the inside and outside of the room. In addition, since the initial air in the main component path is excluded, the object to be dried is not oxidized by oxygen during drying, and the clothes can be dried easily.
[0020]
Therefore, according to the present invention, it is possible to provide a superheated steam drying method and apparatus that can improve the thermal efficiency and save energy, and that do not discharge an off-flavor to the outdoors because an exhaust duct is not used.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an outline of a superheated steam dryer according to the present invention.
FIG. 2 is a configuration diagram showing an alternative example of the superheated steam dryer according to the present invention.
FIG. 3 is a configuration diagram showing an outline of a conventional push-in drum type drying apparatus.
FIG. 4 is a configuration diagram showing an outline of a conventional suction-type drum-type drying apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Drying drum 2 Door 3 Circulation duct 4 Circulation fan 5 Superheater heater 6 Steam supply pipe 7 Steam supply valve 10 Bypass pipe 11 Check valve 12 Capacitor 13 Automatic valve A
14 Airbag 15 Air supply blower 16 Automatic valve B
20 Dried object 31 Air supply fan 32 Heater 33 Drying drum 34 Exhaust duct 35 Waste thread removal filter

Claims (5)

被乾燥物を乾燥させるドラム式乾燥機において、乾燥ドラムと循環ダクトとを含んでなる主構成経路に蒸気を供給しつつ、該主構成経路内に初期からあった空気を該主構成経路外の空気貯留手段に導き、該主構成経路を閉回路にした後、該主構成経路内で過熱蒸気を循環させることによって該被乾燥物の水分を蒸発させることを特徴とする過熱蒸気式乾燥方法。In a drum dryer for drying an object to be dried, while supplying steam to a main constituent path including a drying drum and a circulation duct, air from the beginning in the main constituent path is removed from the main constituent path. A superheated steam type drying method characterized by evaporating moisture of the material to be dried by circulating the superheated steam in the main constituent path after guiding the air to the air storage means and making the main constituent path into a closed circuit. 上記過熱蒸気が100℃〜150℃の温度範囲にある請求項1記載の過熱蒸気式乾燥方法。The superheated steam drying method according to claim 1, wherein the superheated steam is in a temperature range of 100C to 150C. 上記被乾燥物の水分が蒸発することによって該主構成経路内の圧力が上昇するが、その内圧の上昇分のみの蒸気を冷却して凝縮水として回収し、排ガスを屋外に放出しないことを特徴とする請求項1又は2記載の過熱蒸気式乾燥方法。Although the pressure in the main component path rises due to the evaporation of the moisture of the material to be dried, the steam of only the increase in the internal pressure is cooled and recovered as condensed water, and the exhaust gas is not released outdoors. The superheated steam drying method according to claim 1 or 2. 被乾燥物を攪拌する乾燥ドラムと、該乾燥ドラムの出口と入口をつなぐ循環ダクトと、該循環ダクトに設置された循環ファン及び過熱ヒータと、該循環ダクトに接続された蒸気供給管と、該循環ダクトの一部分を迂回するように該循環ダクトの一位置と他の位置を結ぶバイパス管と、該バイパス管に設けられた該乾燥ドラム及び該循環ダクト内の空気を保留するための空気貯留手段と、該バイパス管又は該循環ダクトに設けられた冷却用のコンデンサとを含んでなり、該乾燥ドラムと該循環ダクトとを含んでなる主構成経路が閉回路であることを特徴とする過熱蒸気式乾燥装置。A drying drum that stirs the material to be dried, a circulation duct that connects an outlet and an inlet of the drying drum, a circulation fan and a superheater installed in the circulation duct, a steam supply pipe connected to the circulation duct, A bypass pipe connecting one position of the circulation duct to another position so as to bypass a part of the circulation duct, the drying drum provided in the bypass pipe, and an air storage means for retaining air in the circulation duct And a condenser for cooling provided in the bypass pipe or the circulation duct, and the main constituent path including the drying drum and the circulation duct is a closed circuit, Type drying equipment. 請求項4記載の過熱蒸気式乾燥装置を含んでなるドラム式洗濯乾燥装置。A drum-type washing and drying apparatus comprising the superheated steam drying apparatus according to claim 4.
JP2001156303A 2001-05-25 2001-05-25 Superheated steam drying method and apparatus Expired - Fee Related JP4516704B2 (en)

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US9663894B2 (en) 2005-11-10 2017-05-30 Lg Electronics Inc. Steam generator and laundry dryer having the same and controlling method thereof
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JPS6173699A (en) * 1984-09-18 1986-04-15 シャープ株式会社 Cloth drying method
JPH01146586A (en) * 1987-12-03 1989-06-08 Fuji Car Mfg Co Ltd Dry cleaning machine
JPH02149297A (en) * 1988-11-30 1990-06-07 Mitsubishi Heavy Ind Ltd Dry-cleaning method
JP2001000792A (en) * 1999-06-22 2001-01-09 Koei Kogyo Kk Dryer for textile product

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Publication number Priority date Publication date Assignee Title
JPS6173699A (en) * 1984-09-18 1986-04-15 シャープ株式会社 Cloth drying method
JPH01146586A (en) * 1987-12-03 1989-06-08 Fuji Car Mfg Co Ltd Dry cleaning machine
JPH02149297A (en) * 1988-11-30 1990-06-07 Mitsubishi Heavy Ind Ltd Dry-cleaning method
JP2001000792A (en) * 1999-06-22 2001-01-09 Koei Kogyo Kk Dryer for textile product

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