JPS6280485A - Drier - Google Patents

Drier

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Publication number
JPS6280485A
JPS6280485A JP22139885A JP22139885A JPS6280485A JP S6280485 A JPS6280485 A JP S6280485A JP 22139885 A JP22139885 A JP 22139885A JP 22139885 A JP22139885 A JP 22139885A JP S6280485 A JPS6280485 A JP S6280485A
Authority
JP
Japan
Prior art keywords
air
heat exchanger
temperature
refrigerator
evaporator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP22139885A
Other languages
Japanese (ja)
Inventor
内田 四市郎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHIYOUNETSUGAKU KENKYUSHO KK
Original Assignee
SHIYOUNETSUGAKU KENKYUSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHIYOUNETSUGAKU KENKYUSHO KK filed Critical SHIYOUNETSUGAKU KENKYUSHO KK
Priority to JP22139885A priority Critical patent/JPS6280485A/en
Publication of JPS6280485A publication Critical patent/JPS6280485A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 ■)・・・産業上の利用分野 本発明は、庫体内に収納した、主として、穀類(米、麦
、豆など)、種子類、その他の農産物(干いも、しいた
け、煙草、薬草など)、海産物、木材、等々のものを、
特に比較的高温(例、60〜80℃内外)で効率的に乾
燥する乾燥装置に係るものであり、また、比較的低温(
例、5〜15℃内外)乃至常温(例15〜40℃内外)
でも効率的な乾燥を行い得る乾燥装置に係るものである
DETAILED DESCRIPTION OF THE INVENTION ■)...Industrial Field of Application The present invention is mainly applicable to grains (rice, wheat, beans, etc.), seeds, and other agricultural products (dried potatoes, shiitake mushrooms, etc.) stored in a warehouse. , tobacco, medicinal herbs, etc.), seafood, wood, etc.
In particular, it relates to drying equipment that efficiently dries at relatively high temperatures (e.g., around 60 to 80 degrees Celsius), and also at relatively low temperatures (
Example: 5-15℃) to room temperature (Example: 15-40℃)
However, it relates to a drying device that can perform efficient drying.

■)・・・前提技術 出願人は先に、特願昭57−193072号、「冷凍機
と熱交換器による乾燥システム」、同昭59−4318
6号、「除湿乾燥器」によって、除湿作用に優れた各種
冷凍機を応用してその構成機器を特殊配設すると共に、
これに熱交換器を特定の循環経路を形成する企図のもと
に組合せて構成した、特に、この種従来の乾燥装置と異
なり、庫内の乾燥空気を高温に保ちつつ、しかも冷凍機
を理想状態で長時間連続運転可能としたごとを最大の特
長とする乾燥装置の発明をなし、特許出願しているもの
であるが、 本願発明は、上記乾燥装置における熱交換器を、第1、
第2熱交換器の2段構えとしたものであり、それによっ
て、熱交換作用を前出願の1基だけのように一気に行わ
ずに、段階的に行うようにして、もって、熱交換の効率
を高め、特に除湿乾燥能力を顕著に向−トすることに成
功したものである。
■) ... The applicant of the underlying technology previously filed Japanese Patent Application No. 57-193072, ``Drying System Using Refrigerator and Heat Exchanger,'' Japanese Patent Application No. 59-4318.
No. 6, the "dehumidifying dryer" applies various types of refrigerators with excellent dehumidifying properties and specially arranges its component equipment,
This is combined with a heat exchanger to form a specific circulation path.In particular, unlike conventional drying equipment of this kind, it maintains the dry air inside the refrigerator at a high temperature, while also making it ideal for refrigerators. The inventor has invented a drying device whose main feature is that it can be operated continuously for a long time under the conditions, and has applied for a patent.
The second heat exchanger has a two-stage arrangement, and thereby the heat exchange action is not carried out all at once as in the case of only one unit in the previous application, but is carried out in stages, thereby increasing the efficiency of heat exchange. In particular, we have succeeded in significantly improving the dehumidifying and drying ability.

■)・・・構成 本発明乾燥装置の構成をその実施例につき説明すれば、
圧縮器1、蒸発器2、凝縮器3、レシーバ−タンク、ア
ノキュームレータ及ヒ膨張弁等からなる圧縮式冷凍機(
実施例ば、200V、1.5 Kw、2HPのものを使
用)や、吸収式冷凍機その他の既存構成の各種冷凍機を
応用して被乾燥物を収納した庫内空気の除湿を行い、も
って、被乾燥物を乾燥する方式において、 ドア4を備えた断熱パネル5等で構成した断熱密閉構成
の庫体6 (例、容積約4.3 m)の内部または外部
(天井板上など)に、断熱構成のハウジング7を適宜設
置し、該ハウジング7内に、冷凍機の一部たる蒸発器2
と加熱器3a(凝縮器3または電気ヒータ等)を、両者
間に適宜構成の第1熱交換器8a及び第2熱交換器8b
を介在して設置し、 第1熱交換器8aの−il+に吸気口9を設けると共に
他側と第2熱交換器8bの→側との間に通気路10aを
設け、該第2熱交換器8bの他側と蒸発器2の前面との
間に通気路10bを設け、また、加熱器3aの後方に排
気口11を設けて構成して、 上記庫体6内の空気の一部を、吸気ファン12等による
適宜の吸気若しくは送気手段にて、第1熱交換器8a−
第2熱交換器8b−蒸発器2−第2熱交換器8b−第1
熱交換器8a−加熱器3aの順に通過せしめるようにし
たものである。
■)...Structure The structure of the drying apparatus of the present invention will be explained with reference to its embodiments.
A compression refrigerating machine consisting of a compressor 1, evaporator 2, condenser 3, receiver tank, annocuumulator, expansion valve, etc.
For example, a 200 V, 1.5 Kw, 2 HP), absorption type refrigerator, and other refrigerators with existing configurations are applied to dehumidify the air inside the refrigerator containing the items to be dried. , in the method of drying the material to be dried, inside or outside (on the ceiling board, etc.) a storage body 6 (e.g., volume approximately 4.3 m) with an insulated and sealed structure consisting of an insulating panel 5 equipped with a door 4, etc. , a housing 7 having a heat-insulating structure is appropriately installed, and an evaporator 2, which is a part of a refrigerator, is installed in the housing 7.
and a heater 3a (condenser 3 or electric heater, etc.), and a first heat exchanger 8a and a second heat exchanger 8b configured as appropriate between the two.
An air inlet 9 is provided at -il+ of the first heat exchanger 8a, and an air passage 10a is provided between the other side and the → side of the second heat exchanger 8b, and the second heat exchanger A ventilation path 10b is provided between the other side of the container 8b and the front surface of the evaporator 2, and an exhaust port 11 is provided at the rear of the heater 3a, so that a part of the air in the storage body 6 can be removed. , the first heat exchanger 8a- by an appropriate intake or air supply means such as the intake fan 12
Second heat exchanger 8b-evaporator 2-second heat exchanger 8b-first
It is made to pass through the heat exchanger 8a and the heater 3a in this order.

上記装置において、 (i)、13はドレンパンであり、蒸発器2、第2熱交
換器8bの冷却結露による除湿作用で生じた水滴を処理
する。
In the above apparatus, (i), 13 is a drain pan, which processes water droplets generated by the dehumidification effect due to cooling condensation of the evaporator 2 and the second heat exchanger 8b.

(ii)、加熱器3aの一例としての上記凝縮器3は、
主として低温乃至常温の乾燥システムの場合には設置し
ない場合もあり、また、本発明装置内に設置せず庫外側
等に設置する場合もある。
(ii) The condenser 3 as an example of the heater 3a is
In the case of a drying system that operates mainly at a low temperature or room temperature, there are cases where it is not installed, and there are cases where it is not installed inside the apparatus of the present invention but is installed outside the refrigerator.

更に、凝縮器3と電熱ヒータ等の適宜のヒータを組合せ
て設置する場合も、そのどちらか一方だけを設置する場
合もある。
Further, the condenser 3 and an appropriate heater such as an electric heater may be installed in combination, or only one of them may be installed.

(iii)、また、図示例は、本発明装置を備えたハウ
ジング7を庫体Gの天井板上に設置したちのであるが、
例えば庫体の内部または外部側面等に設置しても、また
庫体と分離して設置しても、その吸気口9と排気口11
を庫体6内部と連通ずれば、全(同様である。
(iii) Also, in the illustrated example, the housing 7 equipped with the device of the present invention is installed on the ceiling board of the storage body G.
For example, the intake port 9 and the exhaust port 11 may be installed inside or on the external side of the storage unit, or even if installed separately from the storage unit.
If it communicates with the inside of the storage body 6, the whole (same).

(iv)、冷凍機の他の構成機器、例えば圧縮式冷凍機
における圧縮器1、レシーバ−タンク、アソキュムレー
ター及び、補助凝縮器3b等は、本発明装置に近接々続
して庫体6の天板上等に適宜設置する。
(iv) Other components of the refrigerator, such as a compressor 1, a receiver tank, an assemblator, and an auxiliary condenser 3b in a compression refrigerator, are connected closely to the storage body 6 of the present invention. Place it on the top plate, etc., as appropriate.

(■)、第1及び第2の熱交換器8a、8bは、上記の
如く、吸気口9から蒸発器2前面へ通す高温庫内空気と
、蒸発器2を通った冷却空気とを熱交換するものである
から、既存構成の所謂熱交換器であれば可であって、そ
の具体的構成は全く任意であるが、例えば、図示はしな
いが小間隔に平行した波形を形成した多数の薄いアルミ
波形板を、中間に仕切平板を介して、直角方向に交互に
交叉積層して方形プロ・ツク状に構成したものを用いる
(■) As described above, the first and second heat exchangers 8a and 8b exchange heat between the high-temperature chamber air that passes from the intake port 9 to the front of the evaporator 2 and the cooling air that has passed through the evaporator 2. Therefore, it is possible to use a so-called heat exchanger with an existing configuration, and its specific configuration is completely arbitrary. A rectangular block-like structure is used in which aluminum corrugated plates are alternately stacked crosswise in the right angle direction with a partition plate in the middle.

(vi)、補助凝縮器3bは、庫体6外に適宜設置し、
装置内の凝縮器3が主に空気加温用の加熱用として作用
する場合に、冷凍機本来の凝縮作用の不足を補うことを
主に行わしめる。
(vi) The auxiliary condenser 3b is appropriately installed outside the storage body 6,
When the condenser 3 in the device mainly functions for heating air, it is mainly used to compensate for the lack of condensing function inherent in the refrigerator.

(vii)、庫体6内は、例えば乾燥効率を良くするた
めに、乾燥室14の周囲を多孔板15その他で区画し、
通風路16を形成し、また環流ファン17、補助ヒータ
18等を設置するなどして、庫内空気が庫内全体を万遍
なく環流し、高温乾燥空気が乾燥室14内の被乾燥物に
むらなく接触して、均一な乾燥が行われるように設ける
(vii) Inside the storage body 6, for example, the periphery of the drying chamber 14 is partitioned with a perforated plate 15 or the like in order to improve drying efficiency;
By forming a ventilation path 16 and installing a circulation fan 17, an auxiliary heater 18, etc., the air inside the refrigerator circulates evenly throughout the interior of the refrigerator, and high-temperature dry air reaches the items to be dried in the drying chamber 14. Provide even contact to ensure uniform drying.

■)・・・作用 次に、上記の構成におりる本発明装置の作用につき説明
すると、 高温高温庫内空気(例、60〜80℃位の場合、但し、
無負荷時)を第1熱交換器8aを通し熱交換して温度低
下(40〜50℃位)し、次で第2熱交換器8bを通し
熱交換して冷凍機能力の適温に温度低下(20〜25℃
位)したのち蒸発器2を通して冷却(12〜17゛C位
)し同時に除湿し、この蒸発器2を通って冷却除湿され
た空気を前記第2及び第1熱交換器78b、8伐を通し
熱交換〔前記高温庫内空気(60〜80℃位)を温度低
下(20〜25℃位)すると共に、蒸発器2を通った冷
却除湿空気(12〜17°C位)を加?IA (43〜
53°C位)する熱交換作用。〕を行い、この加温空気
を加熱器3aを通して目的庫内温度(60〜80°C位
)に温度上昇して、再び庫体6内へ戻して、上記空気循
環によって庫内空気の加温と除湿を極めて有効に行い、
もって、庫内に収納した被乾燥物の乾燥を極めて効果的
に行うようにしたものである。
■)...Function Next, the function of the device of the present invention having the above configuration will be explained.
(at no load) through the first heat exchanger 8a to lower the temperature (about 40 to 50 degrees Celsius), then through the second heat exchanger 8b to exchange heat to lower the temperature to the appropriate temperature for the refrigeration function. (20~25℃
After that, the air is cooled (to about 12-17°C) through the evaporator 2 and dehumidified at the same time, and the cooled and dehumidified air is passed through the second and first heat exchangers 78b and 8. Heat exchange [The temperature of the high-temperature warehouse air (about 60 to 80 degrees Celsius) is lowered (to about 20 to 25 degrees Celsius), and the cooled dehumidified air (about 12 to 17 degrees Celsius) that has passed through the evaporator 2 is added? IA (43~
Heat exchange effect (approximately 53°C). ], the heated air is raised to the target internal temperature (approximately 60 to 80°C) through the heater 3a, and returned to the storage body 6, and the air inside the refrigerator is heated by the above-mentioned air circulation. and extremely effective dehumidification,
As a result, the drying material stored in the refrigerator can be dried extremely effectively.

■)・・・実施例による各種データ (i)  ・・・第4図は、上記本発明実施例装置(第
1図、第3図、冷凍機・・−200V、1.5 Kw、
211P、庫内容積約4.3 M)において、第1、第
2熱交換器を中心とした下記の各位置における温度変化
を表わすグラフであり、 これを、第5図の出願人が先に特許出願した先発明実施
例装置(第2図参照、即ち、熱交換器は1基だけ)の、
本発明と全く同条件における、各位置の温度変化を表わ
すグラフと比較すると、熱交換器による温度降下能力に
おいて両者に差異があり、本発明装置が明らかに改良さ
れていることを直ちに理解し得る。
■) ...Various data (i) ...Fig. 4 shows the above-mentioned apparatus according to the present invention (Fig. 1, Fig. 3, refrigerator...-200V, 1.5 Kw,
This is a graph showing the temperature changes at the following positions centering on the first and second heat exchangers in 211P, the internal volume of which is approximately 4.3 M), and the applicant of Fig. 5 first proposed this graph. The device according to the earlier invention for which a patent application has been applied (see Figure 2, that is, there is only one heat exchanger),
When compared with a graph showing the temperature change at each location under exactly the same conditions as the present invention, it can be immediately understood that there is a difference in the temperature reduction ability of the heat exchanger between the two, and that the device of the present invention is clearly improved. .

(A>・・・・吸気口9、第1熱交換器8a入口(即ち
、庫内温度)。
(A>...Intake port 9, first heat exchanger 8a inlet (i.e., internal temperature).

(B)・・・・(A)から第1熱交換器8aを通って出
た位置(熱交換−冷却)。
(B)...The position exiting from (A) through the first heat exchanger 8a (heat exchange-cooling).

(C)・・・・(B)から第2熱交換器8bを通って出
た位置(熱交換−冷却)。
(C)...The position exiting from (B) through the second heat exchanger 8b (heat exchange-cooling).

(D)・・・・(C)から蒸発器2を通って出た位置(
冷却)。
(D)...The position exiting from (C) through the evaporator 2 (
cooling).

(E)・・・・(D)から第2熱交換器8bを通って出
た位置(熱交換−加温)。
(E)...The position exiting from (D) through the second heat exchanger 8b (heat exchange - heating).

(F)・・・・(E)から第1熱交換器8aを通って出
た位置(熱交換−加温)。
(F)...The position exiting from (E) through the first heat exchanger 8a (heat exchange-heating).

(G)・・・・(F)から加熱器3aを通って出た位W
(加温)。
(G)...The part W that exited from (F) through the heater 3a
(Warming).

(、H)・・・・(F)から補助ヒータ8を通って出た
位置(目的庫内温度に調節加温)。
(, H)...The position exiting from (F) through the auxiliary heater 8 (adjusted and heated to the target internal temperature).

(注)1、先発明(第2図、第5図)は、(B)、(E
)が無い。
(Note) 1. Prior inventions (Fig. 2, Fig. 5) are (B), (E
) is missing.

(注)2、上記は無負荷時、即ち、庫内に含水被乾燥物
を入れていない場合である。
(Note) 2. The above is when there is no load, that is, when there is no moisture-containing material to be dried in the refrigerator.

後記の如く、庫内に被乾燥物を入れ て負荷を加えた場合及び、冷凍機の能 力、庫体容積の大小等によって、当然 に数値は変ってくる。As described below, put the items to be dried in the refrigerator. When a load is applied, the function of the refrigerator Naturally, it depends on the force, the size of the storage body, etc. The numbers will change.

(ii )  ・・・第6図、第7図及び第8図の各グ
ラフは、上記の本発明(第4図)と先発明(第5図)の
差異を明確に把握するために、庫体温度が40“C16
0℃及び80℃の各場合を摘出対比したものであり、こ
れによって、特に、両者の熱交換作用時における降下温
度差がはっきりと表われる。
(ii)...The graphs in Figures 6, 7, and 8 are drawn in order to clearly understand the differences between the present invention (Figure 4) and the prior invention (Figure 5). Body temperature is 40"C16
This is a comparison of the cases of 0°C and 80°C, which clearly shows the difference in temperature drop during heat exchange between the two cases.

而して、この温度差が第10図における庫内湿度の差及
び、第11図における除湿量の差の原因をなすものであ
り、本発明装置が先発明装置に比し、格段に高い除湿乾
燥能力を有することを証明するものである。
This temperature difference is the cause of the difference in internal humidity in Figure 10 and the difference in dehumidification amount in Figure 11, and the device of the present invention has a much higher dehumidification rate than the previous device. This proves that the product has drying ability.

(iii )  ・・・第9図は、負荷実施例として、
上記本発明実施例装置において、毛布片(例、10×l
 Q cmのもの数10枚)に水を吸わせて、水分共合
針100 kgとしたものを、乾燥室14内の棚にほぼ
均等に並べた場合における、庫内温度、庫内湿度及び除
湿水量(蒸発器2、第2熱交換器8bによる冷却作用時
の結露水滴をドレンパン13から庫外へ排出した水量)
の、経時変化を表わすグラフである。
(iii)...Figure 9 shows, as a load example,
In the apparatus according to the embodiment of the present invention, a piece of blanket (for example, 10×l
The temperature, humidity, and dehumidification inside the refrigerator when 100 kg of water absorbing needles (10 sheets of Q cm) are soaked with water and are arranged almost evenly on a shelf in the drying room 14. Amount of water (amount of water that drains condensed water droplets from the drain pan 13 to the outside of the refrigerator during the cooling action of the evaporator 2 and the second heat exchanger 8b)
It is a graph showing the change over time.

この場合も、加熱器3a、補助し−タ1Bを通って庫内
へ戻される空気温度は80℃内外であるが、被乾燥物(
含水毛布片)に触れて温度低下して、グラフ表示の時点
では庫内温度40゛C内外となっている。しかし、被乾
燥物が完全に除湿乾燥される時点(約20時間経過)で
は70〜80℃に達する。
In this case as well, the temperature of the air returned to the refrigerator through the heater 3a and the auxiliary heater 1B is around 80°C, but the material to be dried (
The temperature of the refrigerator dropped when it touched the water-containing blanket, and at the time the graph was displayed, the temperature inside the refrigerator was around 40°C. However, when the material to be dried is completely dehumidified and dried (approximately 20 hours have elapsed), the temperature reaches 70 to 80°C.

(iv)  ・・・第10図は、上記負荷実施例におけ
る、本発明と先発明の庫内温度の経時的減少を対比して
表わしたグラフであり、 また、第11図は、除湿量の経時的基Aヒを対比して表
わしたグラフである。
(iv)...Figure 10 is a graph comparing the decrease in internal temperature over time between the present invention and the previous invention in the above load example, and Figure 11 is a graph showing the decrease in the amount of dehumidification over time. It is a graph showing a comparison of groups A and H over time.

これによって、前記(11)項に記したように、両者の
熱交換器による熱交換能力の差がそのまま湿度減少即ち
除湿量の増加となって表われていることがわかる。
This shows that, as described in item (11) above, the difference in heat exchange ability between the two heat exchangers directly manifests itself as a decrease in humidity, that is, an increase in the amount of dehumidification.

なお、本発明装置において、空気中の水分が結露し水滴
となって除去されるのは、第2熱交換器8b及び凝縮器
2においてであって、第1熱交換器8aにおいては熱交
換は効果的に行われるが水分の除去作用はあまり行われ
ない。これは、庫内から直ちに第1熱交換器3aへ入る
空気温度が高すぎるためと考えられる。
In the apparatus of the present invention, moisture in the air is condensed and removed as water droplets in the second heat exchanger 8b and condenser 2, and heat exchange is not performed in the first heat exchanger 8a. Although it is effective, the water removal action is not very effective. This is considered to be because the temperature of the air that immediately enters the first heat exchanger 3a from inside the refrigerator is too high.

このことからして、先発明が1基の熱交換器だけで行っ
ていたために、充分有効な熱交換作用、特に除湿作用を
発揮し得ながったこ点がわかり、併せて、本発明が熱交
換器を第1及び第2の2段構えとしたことの成果が明白
に立証されるものである。
From this, it can be seen that since the previous invention used only one heat exchanger, it was not possible to exhibit a sufficiently effective heat exchange action, especially a dehumidifying action. This clearly demonstrates the effectiveness of having a two-stage heat exchanger arrangement, the first and second stages.

(V)  ・・・第12図は、−ト記第10図に表われ
た本発明と先発明の除湿量の差異を数値で表わしたもの
であり、その増加割合を平均すると約7%となる。
(V)...Figure 12 numerically represents the difference in the amount of dehumidification between the present invention and the prior invention shown in Figure 10 of the section (G), and the average increase rate is approximately 7%. Become.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明装置の構成説明図、第2図は先発明装置
の構成説明図、第3図は本発明の実施例装置の縦断面図
、第4図は本発明実施例装置(第1図、第3図)におけ
る各位置の温度変化を示すグラフ、第5図は先発明実施
例装置(第2図)における各位置の温度変化を示すグラ
フ、第6図、第7図及び第8図は、第4図及び第5図に
おける庫内温度40’c、60°C及び80℃の場合を
取り出して対比したグラフ、第9図は本発明実施例装置
において、負荷を加えた場合の庫内温度、庫内湿度及び
除湿水量の経時変化を表わすグラフ、第10図は負荷実
施例における本発明と先発明の庫内湿度の経時的変化を
対比したグラフ、第11図は同じ(除湿量の経時的変化
を対比したクラブ、第12図は本発明と先発明の除湿量
の差異を数値で表わした表である。 符号、1・・・・冷凍機の圧縮器、2・・・・蒸発器3
・・・・凝縮器、3a・・・・加熱器、3b・・・・補
助凝縮器、4・・・・ドア、5・・・・断熱パネル、6
・・・・庫体、7・・・・ハウジング、8a・・・・第
1熱交換器、8b・・・・第2熱交換器、9・・・・吸
気口、10a、10b・・・・通気路、11・・・・排
気口、12・・・・吸気ファン、13・・・・ドレンパ
ン、14・・・・乾燥室、]5・・・・多孔板、16・
・・・通風路、17・・・・環流ファン、1B・・・・
補助し−タ。 第6図 庫内温度40’C C ■ ◎  @  0  ■  0 本発明 −一一一一一一一 先発明 □ 第7図 庫内温度 60’ C C ■  ◎  ■  ■  ■  0 本発明−−−−−−− 先発明□ ?881882と旭郵 量に謎郵  0
FIG. 1 is an explanatory diagram of the configuration of the device of the present invention, FIG. 2 is an explanatory diagram of the configuration of the prior invention device, FIG. 3 is a vertical cross-sectional view of the embodiment of the device of the present invention, and FIG. 1 and 3), FIG. 5 is a graph showing temperature changes at each position in the device according to the embodiment of the prior invention (FIG. 2), and FIGS. 6, 7, and Figure 8 is a graph comparing the cases of internal temperature 40'C, 60 °C and 80 °C in Figures 4 and 5, and Figure 9 is a graph when a load is applied to the apparatus according to the present invention. Figure 10 is a graph comparing the changes over time in the refrigerator humidity of the present invention and the previous invention in the load example, and Figure 11 is the same ( Fig. 12 is a table that numerically represents the difference in the amount of dehumidification between the present invention and the previous invention.Symbols: 1...Refrigerating machine compressor, 2... ...Evaporator 3
... Condenser, 3a ... Heater, 3b ... Auxiliary condenser, 4 ... Door, 5 ... Heat insulation panel, 6
... Storage body, 7 ... Housing, 8a ... First heat exchanger, 8b ... Second heat exchanger, 9 ... Intake port, 10a, 10b ...・Vent passage, 11...Exhaust port, 12...Intake fan, 13...Drain pan, 14...Drying room, ]5...Perforated plate, 16...
...Ventilation duct, 17...Recirculation fan, 1B...
Assistance. Figure 6 Temperature inside the refrigerator 40' C C ■ ◎ @ 0 ■ 0 Invention -111111 earlier invention □ Figure 7 Temperature inside the refrigerator 60' C C ■ ◎ ■ ■ ■ 0 The present invention --- −−−− First invention□? 881882 and Asahi mail mysterious mail 0

Claims (1)

【特許請求の範囲】[Claims] (1)、既存構成の各種冷凍機を応用して被乾燥物を収
納した庫内空気の除湿を行い、もって、 被乾燥物を乾燥する乾燥方式であり、 庫内空気の一部を、適宜の吸気若しくは送気手段にて、
熱交換器→蒸発器(冷却器)→同一熱交換器→加熱器の
順に通過せしめ、 もって、高温高湿庫内空気を熱交換器を通し熱交換して
冷凍機能力の適温に温度低下したのち蒸発器(冷却器)
を通して冷却除湿し、 この蒸発器(冷却器)を通って冷却除湿された空気を前
記熱交換器を通し熱交換(前記高温高湿庫内空気を冷却
除湿空気で温度低下すると共に、蒸発器(冷却器)を通
った冷却除湿空気を高温高湿庫内空気で加温する熱交換
作用。)を行い、この加温空気を加熱器を通して目的庫
内温度に温度上昇して、再び庫内へ戻して、上記空気循
環によって庫内に収納した被乾燥物の乾燥を行うように
した乾燥装置において、 熱交換器を第1熱交換器と第2熱交換器の2段構えとな
し、庫内空気の一部を適宜の吸気若しくは送気手段にて
、第1熱交換器→第2熱交換器→蒸発器(冷却器)→第
2熱交換器→第1熱交換器→加熱器の順に通過せしめて
、再び庫内へ戻すように構成した、乾燥装置。
(1) This is a drying method that uses various types of refrigerators with existing configurations to dehumidify the air inside the warehouse containing the items to be dried, thereby drying the items to be dried. With the air intake or air supply means,
The air passed through the heat exchanger → evaporator (cooler) → same heat exchanger → heater, and the air inside the high-temperature, high-humidity chamber was exchanged with heat through the heat exchanger, and the temperature was lowered to the appropriate temperature for the refrigeration function. Later evaporator (cooler)
The air that has been cooled and dehumidified through this evaporator (cooler) is passed through the heat exchanger for heat exchange (the temperature of the high-temperature, high-humidity chamber air is lowered with the cooled and dehumidified air, and the air is cooled and dehumidified through the evaporator (cooler). A heat exchange action is performed to heat the cooled dehumidified air that has passed through the cooler) with the high-temperature, high-humidity air inside the refrigerator.The heated air is then raised to the desired temperature inside the refrigerator through the heater, and then returned to the inside of the refrigerator. In the drying device, the drying material stored in the refrigerator is dried by the above-mentioned air circulation. A part of the air is sent to the first heat exchanger → second heat exchanger → evaporator (cooler) → second heat exchanger → first heat exchanger → heater using an appropriate intake or air supply means. A drying device configured to pass through and return to the inside of the refrigerator.
JP22139885A 1985-10-04 1985-10-04 Drier Pending JPS6280485A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22139885A JPS6280485A (en) 1985-10-04 1985-10-04 Drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22139885A JPS6280485A (en) 1985-10-04 1985-10-04 Drier

Publications (1)

Publication Number Publication Date
JPS6280485A true JPS6280485A (en) 1987-04-13

Family

ID=16766131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22139885A Pending JPS6280485A (en) 1985-10-04 1985-10-04 Drier

Country Status (1)

Country Link
JP (1) JPS6280485A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007212093A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2007212092A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2007212090A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2008075987A (en) * 2006-09-22 2008-04-03 Yonden Energy Service Kk Dryer
JP2008261543A (en) * 2007-04-11 2008-10-30 Hoshizaki Electric Co Ltd Drying device
JP2015045476A (en) * 2013-08-29 2015-03-12 Gsk株式会社 Cool air dryer

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007212093A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2007212092A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2007212090A (en) * 2006-02-10 2007-08-23 Hoshizaki Electric Co Ltd Drying device
JP2008075987A (en) * 2006-09-22 2008-04-03 Yonden Energy Service Kk Dryer
JP2008261543A (en) * 2007-04-11 2008-10-30 Hoshizaki Electric Co Ltd Drying device
JP2015045476A (en) * 2013-08-29 2015-03-12 Gsk株式会社 Cool air dryer

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