JP4427241B2 - Storehouse - Google Patents

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Publication number
JP4427241B2
JP4427241B2 JP2002305759A JP2002305759A JP4427241B2 JP 4427241 B2 JP4427241 B2 JP 4427241B2 JP 2002305759 A JP2002305759 A JP 2002305759A JP 2002305759 A JP2002305759 A JP 2002305759A JP 4427241 B2 JP4427241 B2 JP 4427241B2
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Japan
Prior art keywords
air
dehumidifier
drying chamber
regeneration
path
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JP2002305759A
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Japanese (ja)
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JP2004138368A (en
Inventor
宏康 桑澤
義孝 矢島
隆彦 齋藤
秋広 林
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Mitsubishi Electric Corp
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Mitsubishi Electric Corp
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  • Drying Of Solid Materials (AREA)
  • Freezing, Cooling And Drying Of Foods (AREA)
  • Drying Of Gases (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、食品等物品の乾燥保管に供する保管庫に関するものである。
【0002】
【従来の技術】
食品やその他の物品を乾燥保管するための保管庫は大きく分けて、塩化カルシウムやペレット状のシリカゲルの乾燥材に庫内の湿気を吸湿させて庫内を乾燥雰囲気にするものと、吸湿材を備えた除湿部に庫内の空気を循環させて吸湿材に吸湿させて庫内を乾燥雰囲気にするものとがある。ペレット状のシリカゲルを吸湿材として使った保管庫は、水も溜まらず、一度吸湿した吸湿材に熱を加えて放湿させることによって再生させることができる(例えば、特許文献1参照)。
【0003】
【特許文献1】
特開平4―114714号公報
【0004】
【発明が解決しようとする課題】
しかしながら、可逆的な吸放湿機能を備えた吸湿材による保管庫においては、再生時に加熱した庫外(室内)の空気を吸湿材に通し、再び庫外(室内)へ排出するため、再生空気の排出口近傍には、熱影響を受けるような家具類は置けないし、排出口を熱影響を受ける壁面等に近づけて設置することもできない。また、ヒーターによる加熱で消費電力が大きく、ランニングコストが嵩むといった問題点もある。
【0005】
本発明は、係る従来の問題点を解決するためになされたものであって、その課題とするところは、周囲に対する熱影響少なく、ランニングコストの低い保管庫を得ることである。
【0006】
【課題を達成するための手段】
前記課題を達成するために本発明は、外箱と、前記外箱に抜き差し可能な引出し箱と、前記引出し箱は、自在に開閉可能な開閉蓋を設けた密閉箱構造の乾燥室と、前記乾燥室の外に備えた吸着除湿装置で構成し、前記吸着除湿装置は、空気を通す多数の通路を有し、可逆的な吸放湿機能を備えた除湿機と、この除湿器の前記通路に通風させる送風機と、前記除湿器に通す空気を昇温させ得る加熱手段とを組込んだ風路を外郭内に構成し、この風路の吸込口と吹出口をそれぞれ隣接する対形態にして開閉可能に構成し、一方の前記吸込み口から前記風路を経て一方の前記吹出口に至る除湿経路と、他方の前記吸込口から前記風路を経て他方の前記吹出口に至る再生経路とを開閉ダンパ機構によって交互に通断させ、除湿運転と再生運転とを交番させるようにするとともに、前記除湿経路は、区切られた前記乾燥室に連絡できるように構成し、前記再生経路は、前記乾燥室外の空間に連絡できるように構成し、前記加熱手段によって前記除湿器に通す空気を、空気温度上昇値を室温(庫外温度)+50Kで昇温する手段を採用する。
【0008】
【発明の実施の形態】
実施の形態1.
図1〜図5によって示す本実施の形態は、食品等の物品を乾燥保管する保管庫に関するものである。この保管庫は、乾燥室1と乾燥室1内の空気を乾燥雰囲気に加工する吸着除湿装置2とから構成されている。乾燥室1は、前面の開放した外箱3に抜き差しできる引出し式の密閉箱構造として構成され、上部に回動やスライドにより開閉できる開閉蓋4が装着されている(図1,図3参照)。上部での開放は、引出し式の場合には乾燥室1への物品の出し入れがし易く使いやすい。乾燥室1の前面は、図1に示すように外方へ張出しの有る前パネル5で構成され、上部の張出し部分の左右に一つずつ開口部6が設けられている。外箱3には乾燥室1を差込んだ状態で、乾燥室1の開閉蓋4と差込み部分の天板との間に前後方向に続く二列の通風路7が天板の中央に設けられた隔壁8により画成される(図1、図3,図4参照)。この二列の通風路7はそれぞれ乾燥室1の前パネル5の二個の開口部6にそれぞれ連絡している。
【0009】
吸着除湿装置2は、外箱3内における乾燥室1の背後に設けられ、空気を通す直線状の多数の通路9を持つ除湿器10と送風機11と、加熱手段12を主体として構成されている。この除湿器10の通路9に通風させる送風機11と、除湿器10に通す空気を昇温させる加熱手段12とを六面体の外殻内の風路13に組込んで吸着除湿装置2が構成されている(図2参照)。
【0010】
吸着除湿装置2の風路13の吸込口14,15と吹出口16,17はそれぞれ隣接する外殻の二面に対形態に開口されている。外殻内には一方の吸込口14から風路13を経て一方の吹出口16に至る除湿経路と、他方の吸込口15から風路13を経て他方の吹出口17に至る再生経路が設けられている。
【0011】
除湿経路と再生経路の各吸込口14,15と各吹出口16,17は二つの開閉ダンパ機構19によって開閉される。開閉ダンパ機構19は、二つの駆動機構で開閉される。即ち、二個のステッピングモーター20の回転軸上に、吸込口開閉ブレード21と吹出口開閉ブレード22が取付けられて構成される。
【0012】
除湿経路の吸込口14と吹出口16は共に乾燥室1に気密を保持した状態に連絡され、再生経路の吸込口15と吹出口17は、外箱3の二列の通風路7にそれぞれ連絡され、乾燥室1の前パネル5の各開口部6を通じてそれぞれ庫外に連絡している。
【0013】
除湿器10は、セラミックス等の無機質繊維にシリカゲル等の吸湿剤を重合反応を利用して、結合させたコルゲート構造材やハニカム構造材を積層して、被処理空気を通す直線状の多数の通路9が全体にわたって分布する、密度230〜270kg/mの直方体状に構成したもので、可逆的な吸放湿機能を有する。各通路9は平行状でそれらの開口端は全て除湿器10の対向する二面に開口している。この除湿器10の構造は、低圧損なため送風機11を小型化できる。
【0014】
加熱手段12は、正特性サーミスタと熱的に接続された放熱フィンが一体化された構成で、除湿器10の前段において風路13を横断する状態に組付けられている。除湿器10と外殻との間には断熱空気層又は多泡性の断熱樹脂の断熱構造23が設けられ、再生時に効率よく除湿器10を加熱するようになっている。
【0015】
この保管庫の乾燥室1は、開閉ダンパ機構19によって除湿経路と再生経路を交互に開閉させ、除湿器10に除湿過程による除湿運転と再生過程による再生運転とを交番させることにより乾燥雰囲気になる。乾燥室1内の除湿は、ステッピングモーター20を回転させ、再生経路の吸込口15及び吹出口17を、吸込口開閉ブレード21及び吹出口開閉ブレード22によって閉止しておいて、送風機11を運転させることにより常温下で行なわれる。即ち、開放された除湿経路により乾燥室1内に循環気流が形成され、除湿器10を通過するたびに湿気が分子状態で除湿器10に吸着され、乾燥室1内は迅速に乾燥雰囲気になる。
【0016】
水の分子を吸着するにつれ除湿器10の吸着能は低下するので、除湿器10を再生過程において再生させる。除湿器10の再生は、ステッピングモーター20を回転させ、除湿経路の吸込口14及び吹出口16を、吸込口開閉ブレード21及び吹出口開閉ブレード22によって閉止し、送風機11を運転させ、正特性サーミスタに通電させることにより行なわれる。加熱手段12による空気温度上昇値は50Kとなるように設定されていて、約70℃ほどの温度下で再生が行なわれる。即ち、開放された再生経路により庫外の空気が前パネル5の開口部6を経て吸込口15から吸込まれ、放熱板を通過することにより加熱され除湿器10の通路9を通ることで除湿器10の水分子が放出される。
【0017】
除湿器10を再生した空気は高温多湿であるが、庫外へ排出される空気温度は低く、再生時に台所等の室内雰囲気の阻害を抑制できるとともに、空気が排出される周りの家具や建物構造等に熱による悪影響を及ぼさない。
【0018】
ここで、庫外の空気条件を20℃、相対湿度100%とした場合には、絶対湿度0.0147kg/kg(DA)を加熱手段12で加熱昇温させ、20℃+50K=70℃となる。絶対湿度は変化しないので、このときの相対湿度は7%となる。一方、除湿器10の吸着等温・湿度特性は、図5に示すような特性である。図5において縦軸は、除湿器10の含水率を示し、横軸は、除湿器10の温度を示す。パラメータは相対湿度である。今、20℃、100%の点Aと加熱手段12により除湿器10が加熱されたときのB点を結べば、再生過程での加熱により、この線上をA点からB点に移行する。即ち、約19Wt%の含水率から約3Wt%の含水率に低下し、除湿器10内の水分子は約16Wt%放出されることになる。通常、シリカゲルは150℃以上の温度を加えて再生するが、ここでは、室温(庫外温度)+50Kの70℃の温度で十分再生させることができる。図5において、仮に100℃に空気温度を上昇させても、除湿器10の含水率は0Wt%であり、水分子の放出量は10Wt%となるが、70℃の場合と比較しても15%程改善されるものの、100℃まで昇温させるエネルギー及び周囲に与える熱による影響は各段に大きなものとなる。
【0019】
こうして再生された除湿器10に除湿経路を開けて乾燥室1内の空気を通すことにより、再び乾燥室1内の湿気を吸着し、乾燥室1内を乾燥雰囲気にすることができる。除湿器10と外殻との間は断熱空気層又は多泡性の断熱樹脂による断熱構造23となっているので周囲への放熱は少なく加熱効率は良い。
【0020】
除湿過程と再生過程とを交互に繰り返えさせる乾燥運転においては、運転開始時には必ず再生経路の開放による除湿器10の再生から始まるように制御される。こうすることにより停止状態で吸湿し、除湿能の低下している除湿器10の状態から乾燥運転をスタートすることがなく、除湿機能が安定することになる。なお、乾燥運転の開始/停止は、乾燥室1内に設けられた湿度センサーの出力値に基づいて制御手段により行なわれる。
【0021】
除湿運転と再生運転とを交番させる乾燥運転について、その一サイクルの経過時間は約30分とし、再生運転と除湿運転との時間配分を、再生運転については65%、除湿運転については35%に設定されている。乾燥時間は、乾燥室1内の湿度が高湿になったことを湿度センサーが検知し、再生運転から除湿運転に至る経過時間として約30分間は許容される時間である。これは、常温での乾燥状態の食品等が略同一の温度下での高湿下における吸湿量は、例えば冷蔵庫で保管し、室内へ取出したときの低温下から常温下への変化による吸湿量と比較しても、格段に小さいことが実態で、日常においても体験することである。
【0022】
そして、再生運転における加熱手段12の加熱時間と非加熱時間の比率が2対1に設定されている。これは、除湿器10の直線状の通路9を通過する空気の流速が0.1m/秒以下に設定されたときの空気量により、加熱手段12で加熱された空気によりほぼ飽和した状態(昇温50K)に到達する。この空気により、除湿器10を加熱し、除湿器10内に吸着されている水分子を放出させてから、非加熱による再生運転を行なう。これにより、通風により除湿器10の温度を下げて、除湿運転に移行させることができ、乾燥室1内の温度を上昇させることなく常温が可能になる。非加熱による再生運転の時間が短いと除湿器10の温度が高い状態であり、また時間が長いと、折角加熱により除湿器10に吸着した水分子を放出再生した状態から吸湿し、次の除湿運転での水分子の吸着量を減じてしまうことになる。さらに、再生運転における風速を0.1m/秒以下とし、除湿運転における風速を再生運転の風速の約3倍に設定することにより、除湿器10に乾燥室1内の湿気を効率的に吸着させることができる。
【0023】
本実施の形態の保管庫によれば、乾燥室1内を迅速かつ効率的に乾燥雰囲気に維持することができ、乾燥室1内に収納した食品等を常温で乾燥保存することができる。そして、水が生じたり、吸湿剤の交換や補充といったメンテナンスも不要であり、扱い易くランニングコストも低く使いやすい。常温乾燥であるため低温乾燥などと異なり、例えば海苔等では庫外に出してからのぱりぱり状態が長持ちし、食味を失いにくい。
【0024】
実施の形態2.
図6〜図10に示す本実施の形態は、実施の形態1で示した保管庫における吸着除湿装置2を前パネル5と乾燥室1との間に嵌込むように構成したもので、基本的な構成は、実施の形態1で示したものと同じである。従って、実施の形態1のものと同じ部分については、実施の形態1のものと同じ符号を用い、それらについての説明は省略する。
【0025】
本実施の形態の保管庫は、吸着除湿装置2が前パネル5と乾燥室1との間に嵌込むように上側に構成されている。吸着除湿装置2の再生経路の吹出口17と吸込口15は外殻の下面に設けられ、設置部の床面側から吸込まれ、床面に向かって吹出される。このような構成を採っても、吹出される空気は50K程度と余り高くないので床面への熱影響は少ない。この場合、図6及び図7に示すように、再生についての吸込口15と吹出口17とに乾燥室1の前面構造24に離反する方向から空気の流入出をするように風向板25を設けると良い。前面構造24がステンレス製やアルミニウム製の場合、冬季の朝など冷込んだ際に前面構造24に直接、再生過程での湿潤状態の空気が触れず、結露を防止することができる。
【0026】
さらには、除湿経路の乾燥室1への吸込口14及び吹出口16に図8に示すよあにスリットやメッシュによる障壁26を設け、異物や物品の吸着除湿装置2内への侵入を防ぐようにしてもよい。また、図9に示すように吸着除湿装置2を乾燥室1の前部下部に設け、吸込口15と吹出口17を直接庫外に連絡させてもよい。こうした構成を採ることにより、乾燥室1の開閉蓋4をスライド式等の間口の広い使い易い構造にすることができ、乾燥室1の気密保持もし易くなる。さらには、図10に示すように、吸着除湿装置2の除湿経路及び再生経路の吸込口14,15と吹出口16,17の位置関係から単一の開閉ダンパ機構19により開閉の切換えができるようにして、保管庫の小型化を図ることもできる。これ以外の機能は上述した実施の形態1のものと同じである。
【0027】
【発明の効果】
この発明によれば、周囲に対する熱影響が少なく、ランニングコストも低減できる効率の良い、食品を常温乾燥で保管できる保管庫が得られる。
【図面の簡単な説明】
【図1】 実施の形態1の保管庫の要部を示す斜視図である。
【図2】 実施の形態1の保管庫の吸着除湿装置を示す断面図である。
【図3】 実施の形態1の保管庫の要部を示す縦断側面図である。
【図4】 実施の形態1の保管庫の要部を示す正面図である。
【図5】 実施の形態1の除湿器の吸着温度・湿度特性図である。
【図6】 実施の形態2の保管庫の斜視図である。
【図7】 実施の形態2の保管庫における要部の縦断面図である。
【図8】 実施の形態2の保管庫における要部の正面図である。
【図9】 実施の形態2の他の保管庫を示す斜視図である。
【図10】 実施の形態2の保管庫の他の吸着除湿装置を示す断面図である。
【符号の説明】
1 乾燥室、 2 吸着除湿装置、 9 通路、 10 除湿器、 11 送風機、 12 加熱手段、 13 風路、 14,15 吸込口、 16,17吹出口、 19 開閉ダンパ機構、 25 風向板、 26 障壁。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to coercive pipe box that Kyosu the dry storage of foods article.
[0002]
[Prior art]
Storage for drying and storing food and other items is broadly divided into a dry atmosphere of calcium chloride or pellet-like silica gel that absorbs moisture in the storage to create a dry atmosphere, and a hygroscopic material. There are some which circulate the air in the warehouse to the dehumidifying part provided to make the moisture absorbent absorb the moisture and make the interior dry. A storage that uses pellet-like silica gel as a hygroscopic material does not accumulate water, and can be regenerated by applying heat to the hygroscopic material that has once absorbed moisture to dehumidify (see, for example, Patent Document 1).
[0003]
[Patent Document 1]
Japanese Patent Laid-Open No. 4-114714 [0004]
[Problems to be solved by the invention]
However, in a storage with a moisture absorbent material having a reversible moisture absorption / release function, the air outside the room (indoor) heated during regeneration passes through the moisture absorbent and is discharged again outside the room (indoor). Furniture that is affected by heat cannot be placed in the vicinity of the outlet, and the outlet cannot be placed close to a wall or the like that is affected by heat. In addition, there is a problem that the power consumption is large due to heating by the heater and the running cost is increased.
[0005]
The present invention was made to solve the conventional problems of, and has as its object is to obtain rather small thermal effect on the surrounding, the low running cost depot.
[0006]
[Means for achieving the object]
To achieve the above object, the present invention provides an outer box, a drawer box that can be inserted into and removed from the outer box, the drying box having a closed box structure provided with an openable / closable lid, and An adsorption dehumidification device provided outside the drying chamber, the adsorption dehumidification device having a plurality of passages through which air passes, and a dehumidifier having a reversible moisture absorption / release function, and the passages of the dehumidifier An air passage incorporating a blower to be ventilated and a heating means capable of raising the temperature of the air passing through the dehumidifier is configured in the outer shell, and the air inlet and the air outlet of the air passage are respectively formed in adjacent pairs. A dehumidification path that is configured to be openable and closable, from one of the suction openings to the one outlet through the air passage, and a regeneration path from the other suction opening to the other outlet through the air passage. Alternates between dehumidifying operation and regenerative operation by alternately switching on and off with an open / close damper mechanism Thereby to cause the dehumidification path, configured to allow communication with said drying chamber, separated, the reproduction path, the dry outdoor configured to be contacted to the space, the dehumidifier by said heating means The means for raising the temperature of the air passing through the air temperature by the air temperature rise value at room temperature (outside temperature) + 50K is adopted.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Embodiment 1 FIG.
The present embodiment shown in FIGS. 1 to 5 relates to a storage for storing articles such as foods in a dry state. This storage is composed of a drying chamber 1 and an adsorption dehumidifying device 2 that processes the air in the drying chamber 1 into a dry atmosphere. The drying chamber 1 is configured as a drawer-type sealed box structure that can be inserted into and removed from the outer box 3 that is open on the front surface, and an opening / closing lid 4 that can be opened and closed by turning or sliding is mounted on the top (see FIGS. 1 and 3). . Opening at the upper part is easy to use in and out of the drying chamber 1 in the case of a drawer type. As shown in FIG. 1, the front surface of the drying chamber 1 is composed of a front panel 5 that projects outward, and one opening 6 is provided on each side of the upper projecting portion. In the outer box 3, with the drying chamber 1 inserted, two rows of ventilation passages 7 extending in the front-rear direction are provided in the center of the top plate between the opening / closing lid 4 of the drying chamber 1 and the top plate of the insertion portion. It is defined by the partition wall 8 (see FIGS. 1, 3 and 4). The two rows of ventilation passages 7 communicate with the two openings 6 of the front panel 5 of the drying chamber 1.
[0009]
The adsorption dehumidifying device 2 is provided behind the drying chamber 1 in the outer box 3 and mainly includes a dehumidifier 10 having a number of linear passages 9 through which air passes, a blower 11, and a heating means 12. . The adsorption dehumidifier 2 is configured by incorporating a blower 11 for ventilating the passage 9 of the dehumidifier 10 and a heating means 12 for raising the temperature of the air passed through the dehumidifier 10 into the air passage 13 in the outer shell of the hexahedron. (See FIG. 2).
[0010]
The inlets 14 and 15 and the outlets 16 and 17 of the air passage 13 of the adsorption dehumidifier 2 are opened in pairs on two surfaces of the adjacent outer shells. In the outer shell, a dehumidifying path from one suction port 14 through the air passage 13 to the one outlet 16 and a regeneration path from the other inlet 15 through the air passage 13 to the other outlet 17 are provided. ing.
[0011]
The suction ports 14 and 15 and the air outlets 16 and 17 in the dehumidification route and the regeneration route are opened and closed by two open / close damper mechanisms 19. The open / close damper mechanism 19 is opened and closed by two drive mechanisms. That is, the inlet opening / closing blade 21 and the outlet opening / closing blade 22 are mounted on the rotation shafts of the two stepping motors 20.
[0012]
Both the suction port 14 and the outlet 16 of the dehumidification path are connected to the drying chamber 1 in an airtight state, and the suction port 15 and the outlet 17 of the regeneration path are respectively connected to the two rows of ventilation paths 7 of the outer box 3. And communicates with the outside through the openings 6 of the front panel 5 of the drying chamber 1.
[0013]
The dehumidifier 10 is formed by laminating a corrugated structure material or a honeycomb structure material in which a hygroscopic agent such as silica gel is bonded to inorganic fibers such as ceramics using a polymerization reaction, and a plurality of linear passages through which air to be treated passes. 9 is distributed in the whole and is formed in a rectangular parallelepiped shape with a density of 230 to 270 kg / m 3 and has a reversible moisture absorption / release function. Each passage 9 is parallel, and all of the opening ends thereof are open on two opposing surfaces of the dehumidifier 10. Since the structure of the dehumidifier 10 is low pressure loss, the blower 11 can be downsized.
[0014]
The heating means 12 has a configuration in which heat dissipating fins that are thermally connected to a positive temperature coefficient thermistor are integrated, and is assembled in a state of traversing the air passage 13 at the front stage of the dehumidifier 10. Between the dehumidifier 10 and the outer shell, a heat insulating air layer or a heat insulating structure 23 of a foamed heat insulating resin is provided, so that the dehumidifier 10 is efficiently heated at the time of regeneration.
[0015]
The drying chamber 1 of this storage has a dry atmosphere by alternately opening and closing the dehumidification path and the regeneration path by the open / close damper mechanism 19 and causing the dehumidifier 10 to alternate between the dehumidification operation by the dehumidification process and the regeneration operation by the regeneration process. . Dehumidification in the drying chamber 1 is performed by rotating the stepping motor 20 and closing the inlet 15 and the outlet 17 of the regeneration path by the inlet opening / closing blade 21 and the outlet opening / closing blade 22 and operating the blower 11. Is performed at room temperature. That is, a circulating air flow is formed in the drying chamber 1 by the opened dehumidifying path, and moisture is adsorbed to the dehumidifying device 10 in a molecular state every time it passes through the dehumidifying device 10, and the inside of the drying chamber 1 quickly becomes a dry atmosphere. .
[0016]
As the water molecules are adsorbed, the adsorption capacity of the dehumidifier 10 decreases, so that the dehumidifier 10 is regenerated in the regeneration process. To regenerate the dehumidifier 10, the stepping motor 20 is rotated, the suction port 14 and the blower outlet 16 of the dehumidification path are closed by the suction port opening / closing blade 21 and the blower outlet opening / closing blade 22, the blower 11 is operated, and the positive temperature coefficient thermistor This is done by energizing the current. The air temperature rise value by the heating means 12 is set to be 50K, and regeneration is performed at a temperature of about 70 ° C. That is, the outside air is sucked from the suction port 15 through the opening 6 of the front panel 5 by the opened regeneration path, heated by passing through the heat radiating plate, and passed through the passage 9 of the dehumidifier 10. Ten water molecules are released.
[0017]
The air that has regenerated the dehumidifier 10 is hot and humid, but the temperature of the air discharged to the outside of the cabinet is low, which can suppress the obstruction of the indoor atmosphere such as the kitchen during the regeneration, and the surrounding furniture and building structure from which the air is discharged No adverse effects due to heat.
[0018]
Here, when the outside air condition is 20 ° C. and the relative humidity is 100%, the absolute humidity of 0.0147 kg / kg (DA) is heated by the heating means 12 and becomes 20 ° C. + 50 K = 70 ° C. . Since the absolute humidity does not change, the relative humidity at this time is 7%. On the other hand, the adsorption isothermal / humidity characteristics of the dehumidifier 10 are as shown in FIG. In FIG. 5, the vertical axis represents the moisture content of the dehumidifier 10, and the horizontal axis represents the temperature of the dehumidifier 10. The parameter is relative humidity. Now, if the point A at 20 ° C. and 100% is connected to the point B when the dehumidifier 10 is heated by the heating means 12, the point A is shifted from the point A to the point B by heating in the regeneration process. That is, the water content is reduced from about 19 Wt% to about 3 Wt%, and water molecules in the dehumidifier 10 are released by about 16 Wt%. Usually, silica gel is regenerated by applying a temperature of 150 ° C. or higher. Here, the silica gel can be sufficiently regenerated at a temperature of 70 ° C. of room temperature (outside temperature) + 50K. In FIG. 5, even if the air temperature is raised to 100 ° C., the moisture content of the dehumidifier 10 is 0 Wt% and the amount of water molecules released is 10 Wt%. %, The influence of the energy to raise the temperature up to 100 ° C. and the heat to the surroundings becomes large at each stage.
[0019]
By opening the dehumidifying path to the regenerated dehumidifier 10 and allowing the air in the drying chamber 1 to pass through, the moisture in the drying chamber 1 can be adsorbed again and the drying chamber 1 can be made a dry atmosphere. Between the dehumidifier 10 and the outer shell is a heat insulating structure 23 made of a heat insulating air layer or a multi-bubble heat insulating resin, so that heat radiation to the surroundings is small and heating efficiency is good.
[0020]
In the drying operation in which the dehumidifying process and the regeneration process are alternately repeated, control is performed so as to always start from the regeneration of the dehumidifier 10 by opening the regeneration path at the start of the operation. By doing so, the dehumidifying function is stabilized without starting the drying operation from the state of the dehumidifier 10 in which the moisture is absorbed in the stopped state and the dehumidifying ability is lowered. The start / stop of the drying operation is performed by the control means based on the output value of the humidity sensor provided in the drying chamber 1.
[0021]
For the drying operation that alternates between the dehumidifying operation and the regeneration operation, the elapsed time of one cycle is about 30 minutes, and the time distribution between the regeneration operation and the dehumidifying operation is 65% for the regeneration operation and 35% for the dehumidification operation. Is set. The drying time is an allowable time of about 30 minutes as the elapsed time from the regeneration operation to the dehumidifying operation when the humidity sensor detects that the humidity in the drying chamber 1 has become high. This is because the amount of moisture absorption under high humidity at approximately the same temperature for foods dried at room temperature is the amount of moisture absorption due to changes from low temperature to room temperature when stored in a refrigerator and taken out indoors, for example. Compared to, the reality is that it is much smaller, and it is an experience in daily life.
[0022]
And the ratio of the heating time and the non-heating time of the heating means 12 in the regeneration operation is set to 2: 1. This is because the air flowing through the linear passage 9 of the dehumidifier 10 is almost saturated with the air heated by the heating means 12 due to the amount of air when the flow velocity is set to 0.1 m / second or less (ascending Temperature 50K). The dehumidifier 10 is heated by this air to release water molecules adsorbed in the dehumidifier 10 and then a regeneration operation without heating is performed. Thereby, the temperature of the dehumidifier 10 can be lowered by ventilation and shifted to the dehumidifying operation, and normal temperature can be achieved without increasing the temperature in the drying chamber 1. If the regeneration operation time by non-heating is short, the temperature of the dehumidifier 10 is high, and if the time is long, the water molecules adsorbed to the dehumidifier 10 by corner heating are released from the regenerated state, and the next dehumidification is performed. This reduces the amount of water molecules adsorbed during operation. Furthermore, the humidity in the drying chamber 1 is efficiently adsorbed to the dehumidifier 10 by setting the wind speed in the regeneration operation to 0.1 m / second or less and setting the wind speed in the dehumidification operation to about three times the wind speed in the regeneration operation. be able to.
[0023]
According to the storage of the present embodiment, the inside of the drying chamber 1 can be quickly and efficiently maintained in a dry atmosphere, and the food stored in the drying chamber 1 can be stored dry at room temperature. Further, there is no need for maintenance such as generation of water or replacement or replenishment of the hygroscopic agent, which is easy to handle and low in running cost. Different from low temperature drying because it is dried at room temperature, for example, laver or the like lasts for a long time after being taken out of the box, making it difficult to lose its taste.
[0024]
Embodiment 2. FIG.
The present embodiment shown in FIGS. 6 to 10 is configured such that the adsorption dehumidifying device 2 in the storage shown in the first embodiment is fitted between the front panel 5 and the drying chamber 1. The configuration is the same as that shown in the first embodiment. Therefore, the same parts as those of the first embodiment are denoted by the same reference numerals as those of the first embodiment, and description thereof is omitted.
[0025]
The storage of the present embodiment is configured on the upper side so that the adsorption dehumidifying device 2 is fitted between the front panel 5 and the drying chamber 1. The outlet 17 and the inlet 15 of the regeneration path of the adsorption dehumidifier 2 are provided on the lower surface of the outer shell, and are sucked from the floor surface side of the installation portion and blown toward the floor surface. Even if such a configuration is adopted, the air blown out is not so high as about 50K, so the thermal influence on the floor surface is small. In this case, as shown in FIGS. 6 and 7, a wind direction plate 25 is provided so that air flows in and out from the direction away from the front structure 24 of the drying chamber 1 at the inlet 15 and the outlet 17 for regeneration. And good. When the front structure 24 is made of stainless steel or aluminum, when the front structure 24 is cooled down, such as in the morning in winter, the front structure 24 is not directly touched by wet air during the regeneration process, and condensation can be prevented.
[0026]
Furthermore, as shown in FIG. 8, a barrier 26 made of a slit or mesh is provided at the suction port 14 and the blowout port 16 to the drying chamber 1 of the dehumidifying path so as to prevent foreign matter and articles from entering the adsorption dehumidifying device 2. It may be. Moreover, as shown in FIG. 9, the adsorption dehumidification apparatus 2 may be provided in the front lower part of the drying chamber 1, and the suction inlet 15 and the blower outlet 17 may be directly communicated with the exterior. By adopting such a configuration, the opening / closing lid 4 of the drying chamber 1 can be configured to be easy to use with a wide opening such as a sliding type, and the drying chamber 1 can be easily kept airtight. Furthermore, as shown in FIG. 10, the opening / closing can be switched by a single opening / closing damper mechanism 19 based on the positional relationship between the suction ports 14, 15 and the outlets 16, 17 of the dehumidification path and the regeneration path of the adsorption dehumidifier 2. In this way, the storage can be downsized. Other functions are the same as those of the first embodiment described above.
[0027]
【The invention's effect】
According to the present invention, an efficient storage that can store foods at room temperature is obtained, which has a low thermal effect on the surroundings and can reduce running costs.
[Brief description of the drawings]
FIG. 1 is a perspective view showing a main part of a storage cabinet according to a first embodiment.
FIG. 2 is a cross-sectional view showing the adsorption dehumidifying device of the storage according to the first embodiment.
FIG. 3 is a longitudinal side view showing a main part of the storage of the first embodiment.
FIG. 4 is a front view showing a main part of the storage of the first embodiment.
5 is an adsorption temperature / humidity characteristic diagram of the dehumidifier according to Embodiment 1. FIG.
FIG. 6 is a perspective view of a storage cabinet according to a second embodiment.
FIG. 7 is a longitudinal sectional view of a main part in the storage of the second embodiment.
FIG. 8 is a front view of a main part in the storage of the second embodiment.
FIG. 9 is a perspective view showing another storage in the second embodiment.
10 is a cross-sectional view showing another adsorption dehumidifying device of the storage of Embodiment 2. FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Drying chamber, 2 Adsorption dehumidification apparatus, 9 Passage, 10 Dehumidifier, 11 Blower, 12 Heating means, 13 Air path, 14,15 Suction inlet, 16, 17 outlet, 19 Opening and closing damper mechanism, 25 Wind direction plate, 26 Barrier .

Claims (1)

外箱と、
前記外箱に抜き差し可能な引出し箱と、
前記引出し箱は、自在に開閉可能な開閉蓋を設けた密閉箱構造の乾燥室と、前記乾燥室の外に備えた吸着除湿装置で構成し、
前記吸着除湿装置は、
空気を通す多数の通路を有し、可逆的な吸放湿機能を備えた除湿機と、この除湿器の前記通路に通風させる送風機と、前記除湿器に通す空気を昇温させ得る加熱手段とを組込んだ風路を外郭内に構成し、この風路の吸込口と吹出口をそれぞれ隣接する対形態にして開閉可能に構成し、一方の前記吸込み口から前記風路を経て一方の前記吹出口に至る除湿経路と、他方の前記吸込口から前記風路を経て他方の前記吹出口に至る再生経路とを開閉ダンパ機構によって交互に通断させ、除湿運転と再生運転とを交番させるようにするとともに、前記除湿経路は、区切られた前記乾燥室に連絡できるように構成し、前記再生経路は、前記乾燥室外の空間に連絡できるように構成し、前記加熱手段によって前記除湿器に通す空気を、空気温度上昇値を室温(庫外温度)+50Kで昇温させるようにしたことを特徴とする引出し式保管庫
An outer box,
A drawer box that can be inserted into and removed from the outer box;
The drawer box is composed of a drying chamber having a closed box structure provided with an openable / closable lid, and an adsorption dehumidifying device provided outside the drying chamber,
The adsorption dehumidifier is
A dehumidifier having a large number of passages for passing air and having a reversible moisture absorption / release function, a blower for passing air through the passages of the dehumidifier, and heating means capable of raising the temperature of the air passed through the dehumidifiers The air passage incorporating the air passage is configured in the outer shell, and the air inlet and the air outlet of the air passage are configured to be adjacent to each other and configured to be openable and closable. The dehumidification path leading to the outlet and the regeneration path leading from the other suction port through the air path to the other outlet are alternately cut off by an open / close damper mechanism so that the dehumidifying operation and the regeneration operation are alternated. The dehumidification path is configured to communicate with the partitioned drying chamber , and the regeneration path is configured to communicate with a space outside the drying chamber , and is passed through the dehumidifier by the heating means. Air, air temperature rise value chamber Pull-out vault, characterized in that so as to warm at (refrigerator outside temperature) + 50K.
JP2002305759A 2002-10-21 2002-10-21 Storehouse Expired - Fee Related JP4427241B2 (en)

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