JPH0426853Y2 - - Google Patents
Info
- Publication number
- JPH0426853Y2 JPH0426853Y2 JP16579684U JP16579684U JPH0426853Y2 JP H0426853 Y2 JPH0426853 Y2 JP H0426853Y2 JP 16579684 U JP16579684 U JP 16579684U JP 16579684 U JP16579684 U JP 16579684U JP H0426853 Y2 JPH0426853 Y2 JP H0426853Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ice
- making
- tank
- ice making
- 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.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 138
- 238000001816 cooling Methods 0.000 claims description 27
- 230000007246 mechanism Effects 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 6
- 239000003507 refrigerant Substances 0.000 claims description 5
- 239000002351 wastewater Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 description 26
- 230000008569 process Effects 0.000 description 25
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Production, Working, Storing, Or Distribution Of Ice (AREA)
- Devices For Blowing Cold Air, Devices For Blowing Warm Air, And Means For Preventing Water Condensation In Air Conditioning Units (AREA)
Description
本考案は空水冷兼用型凝縮器に関し、特に、製
氷機等の負荷変動の大きい装置に使用するのに好
適な凝縮器に関するものである。
The present invention relates to an air/water cooling type condenser, and in particular to a condenser suitable for use in devices with large load fluctuations, such as ice makers.
製氷機は、負荷変動が大きく、且つ定期的に製
氷、除氷サイクルを繰り返すために、このような
事情を考慮して、その凝縮器の設計を行わねばな
らない。例えば、製氷機は、通常上水道のような
給水設備に接続され、製氷開始時には上水道から
給水されるので、特に夏期の高温時には、相当熱
い水道水が蒸発器の負荷となり、いわゆる高負荷
運転を行うことになる。この高負荷運転の時間は
給水された製氷用水がほぼ0℃になる迄(約10分
程度)継続され、製氷板に氷が成長し始めると
徐々に負荷が軽くなる。また、各種の補助凝縮器
を用いた構成が実公昭46−3643号、実開昭57−
8481号及び特開昭53−40454号各公報等に提案さ
れている。
Since ice makers have large load fluctuations and regularly repeat ice making and deicing cycles, their condensers must be designed with these circumstances in mind. For example, ice makers are usually connected to a water supply facility, such as a water supply system, and are supplied with water from the water supply when they start making ice, so especially during high temperatures in the summer, the considerably hot tap water becomes a load on the evaporator, resulting in so-called high-load operation. It turns out. This high-load operation time continues until the supplied ice-making water reaches approximately 0°C (about 10 minutes), and as ice begins to grow on the ice-making plate, the load gradually becomes lighter. In addition, configurations using various auxiliary condensers are Utility Model Publication No. 46-3643 and Utility Model Application No. 57-
This method has been proposed in JP-A No. 8481 and Japanese Patent Application Laid-Open No. 53-40454.
しかし、前述の従来の製氷機においては、高負
荷運転を乗り切るために、軽負荷時の無駄をあえ
て無視し、コスト的には高くなるが最大能力時に
合わせた能力の大きい凝縮器を使用していた。
また、前述の補助凝縮器を用いる構成は、構造
が複雑でコスト高であり、結局は補助的な性能し
か持ち合わせていなかつた。
更に、製氷機として重要なことは、ホツトガス
使用時の問題の克服である。つまり、凝縮能力は
必要以上に大きいだけでは不適当で、製氷時及び
除氷時の凝縮器の能力にバランスが取れていなけ
ればならない。例えば、製氷完了後、除氷時にホ
ツトガス弁を開いて圧縮機の高温吐出ガスを蒸発
器に送つて除氷を行う場合、凝縮器の能力にバラ
ンスが取れていないと、ホツトガスとして流れる
べきガスが凝縮され、除氷時間を極端に長くする
ことになり、最悪のケースとしては離氷が不可能
となることがあつた。
従つて、本考案の目的は、全く簡単な構造であ
りながら、製氷時及び除氷時の凝縮能力のバラン
スが取れている凝縮器を提供することである。
However, in the conventional ice maker mentioned above, in order to survive high-load operation, waste at light loads is intentionally ignored, and a condenser with a large capacity is used at maximum capacity, although it costs more. Ta. Further, the configuration using the auxiliary condenser described above has a complicated structure and high cost, and ultimately only has auxiliary performance. Furthermore, what is important for an ice maker is to overcome the problems when using hot gas. In other words, it is inappropriate for the condensing capacity to be simply larger than necessary; the condenser capacity must be balanced during ice making and deicing. For example, if the hot gas valve is opened to send the high-temperature gas discharged from the compressor to the evaporator to remove ice after ice making is completed, if the condenser capacity is not balanced, the gas that should flow as hot gas may This caused condensation, which made the deicing time extremely long, and in the worst case, it became impossible to remove the ice. Therefore, an object of the present invention is to provide a condenser which has a completely simple structure and which has a well-balanced condensing capacity during ice making and deicing.
この目的を達成するため、本考案は、製氷機構
の製氷用水タンクからの水を受けると共に、排水
を放出するための排水部及び溢水を放出するため
のオーバーフロー部を有する受水槽と、前記製氷
機構の冷媒管に接続され前記受水槽内に配設され
た凝縮パイプと、該凝縮パイプを浸漬するほど前
記受水槽内に水がない場合に同凝縮パイプを空冷
しうる位置に設けられた冷却フアンとを備える空
水冷兼用型凝縮器を提供している。
To achieve this objective, the present invention provides a water receiving tank that receives water from an ice making water tank of an ice making mechanism and has a drainage part for discharging waste water and an overflow part for discharging overflow water, and a water receiving tank for receiving water from an ice making water tank of an ice making mechanism. a condensing pipe connected to the refrigerant pipe and arranged in the water tank, and a cooling fan installed at a position where the condensing pipe can be air-cooled when there is not enough water in the water tank to submerge the condensing pipe. We provide an air/water cooled condenser that is equipped with:
受水槽内に水がある場合には、凝縮パイプは水
と水冷式に熱交換し、水がない場合には、凝縮パ
イプは冷却フアンにより通常の空冷式として冷却
され、負荷の変化具合に応じて凝縮能力が変化す
る。
冷却フアンは、受水槽の水中に設置してもよ
く、その場合には、この冷却フアンにより水が攪
拌された冷却が促進される。
When there is water in the water tank, the condensing pipe exchanges heat with the water in a water-cooled manner, and when there is no water, the condensing pipe is cooled by a cooling fan as a normal air-cooled type, depending on the load change. The condensing capacity changes. The cooling fan may be installed in the water in the water tank, and in that case, the cooling fan stirs the water to promote cooling.
次に、本考案の好適な実施例について添付図面
を参照して詳細に説明するが、図中、同一符号は
同一又は対応部分を示すものとする。
第1図において、符号1で示されるものは、
銅、アルミ等の熱伝導の良好な平板で作られた製
氷板であり、この製氷板1の裏面には蒸発器2が
配設される。この蒸発器2と共に製氷機構を構成
するアキユームレータ3、圧縮機4、凝縮パイプ
5、ドライヤ6及びキヤピラリーチユーブ7は、
図示のように銅管(冷媒管)8でループ状に閉回
路として接続されている。圧縮機4の吐出部4a
はホツトガス弁9を介して蒸発器2の吸入部2a
に接続されている。
製氷板1の下方位置には、製氷用水タンク10
が配設され、この製氷用タンク10内に設けられ
た循環ポンプ11は製氷板1の上方位置に配設さ
れた散水器12に接続されており、循環ポンプ1
1を作動させることにより、製氷用水タンク10
内の製氷用水が連続して散水器12より製氷板1
面上に供給される。
製氷用水タンク10上に配設された給水弁13
は外部水道に接続されており、製氷用水タンク1
0内に水を供給することができる。製氷用水タン
ク10に設けられたオーバーフロー管10aから
の溢水は、ホース10bを経て最下位置に配設さ
れた受水槽14内に供給される。このホース10
bからの溢水量は受水槽14に形成された排水部
14aの排水量よりも多いため、除氷工程におい
ては、受水槽14内に排水が貯まり、受水槽14
の上部に形成されたオーバーフロー部14bから
外部に廃棄される。
更に、受水槽14の上方位置においては、冷却
フアン15と出力軸16を有する冷却モータ17
とが図示しない製氷機本体に取り付けられてい
る。また、ほぼ円筒形の流れ案内体18が受水槽
14内の凝縮パイプ5を包囲するように配設され
ている。該流れ案内体18は、底部に開口18a
が形成されると共に、頂部がラツパ状の拡開部1
8bに形成されている。
以上の構成において、本考案による空水冷兼用
型凝縮器を作動させる場合について述べると、圧
縮機4等の製氷機構を作動させ製氷工程に入る
と、散水器12からの製氷用水の散水が開始さ
れ、製氷板1上に氷1aが徐々に形成される。氷
1aが所定の大きさに成長したことを図示しない
公知の製氷サーモスタツト或はフロートスイツチ
等によつて検知すると、製氷工程から除氷工程に
切り替えられ、ホツトガス弁9が開弁されて圧縮
機4のホツトガスを蒸発器2の吸入口2aに供給
することにより、製氷板1が暖められ、製氷板1
に対する氷1aの接触部を僅かに融かして除氷が
行われる。
また、除氷工程に切り替わる際に、前述のホツ
トガス弁9の開弁と同時に、給水弁13が開弁
し、製氷用水タンク10内に次の製氷工程の製氷
用水が給水され、給水に伴う余剰水は製氷用水タ
ンク10のオーバーフロー管10a及びホース1
0bを経て受水槽14内に送られる。除氷工程の
終了は、製氷板1からの氷1aの落下か、この落
下に伴う製氷板1の温度上昇を検知することによ
つて一般的に知ることができ、除氷工程が終了す
ると、ホツトガス弁9及び給水弁13を閉弁する
ことにより冷却フアン15を回転させて次の製氷
工程を開始することになる。
前述の製氷機において、除氷完了時には、蒸発
器2の温度は比較的高く、約15℃位になつてお
り、除氷工程から製氷工程に入つた初期の製氷用
水タンク10の水温は給水弁13から入ってくる
多量の水によつて上昇し、約25℃位にまで上昇し
ているため、製氷工程における初期の状態の蒸発
器2の温度も高くなつており、その凝縮圧力も15
Kg/cm2G〜17Kg/cm2Gと云う高圧になり、圧縮機
4は過負荷となつてその性能に著しい害を及ぼす
ことになる。
本考案の凝縮器はこのような状況下におても十
分な凝縮作用を奏することができるように構成さ
れている。製氷用水タンク10のホース10bを
流下した溢水は受水槽14内に導かれて貯水され
る。この場合、受水槽14内に供給される余剰水
の温度は製氷用水タンク10内の製氷残水(約0
℃)を希釈したものであるので、水温は約10℃〜
約15℃で比較的低温が保たれている。また、受水
槽14内の貯水状況については、排水部14aか
らの排水量がホース10bからの流入量よりも十
分小さくなるように、排水部14aの口径が選択
されているため、排水部14aが常時開状態であ
つても受水槽14内には水が徐々に貯まり、水位
はオーバーフロー部14bに達するまで上昇し続
ける。給水弁13からの給水は除氷中の全期間又
は一部期間にわたつて行われるが、その間に受水
槽14の水位がオーバーフロー部14bまで到達
できるように、給水量、受水槽14の実効容積、
排水部14aの口径(つまり、排水量)が設計さ
れている。
従つて、製氷開始時には、受水槽14は製氷残
水の希釈水で満水状態であるため、凝縮パイプ5
はその冷水により水冷凝縮器として十分に冷却さ
れ、高い凝縮能力を有している。つまり、製氷開
始時の高負荷時運転における凝縮能力は十分であ
るので、高圧とならず圧縮機4にかかる負荷もか
なり軽減される。更に、製氷工程が継続すると、
受水槽14内の水温が上昇するが、冷却フアン1
5の回転によつて水表面からの蒸発が促進され、
水の蒸発による潜熱によつて水温上昇が抑えられ
る。この間に、受水槽14の排水部14aからは
徐々に排水が行われ、水が全て排水されると共
に、外気が流れ案内体18の外側から矢印A,
B,Cで示される順に流入し、凝縮パイプ5は外
気と熱交換を行うことになる。この場合、受水槽
14の壁面及び凝縮パイプ5に付着した水は蒸発
し、蒸発潜熱によつて凝縮パイプ5が一層冷却さ
れる。
かくして、製氷工程後期には、受水槽からは全
ての水がなくなつて乾燥状態となり、単なる空冷
凝縮器として作動する。この状態は除氷工程にと
つて極めて重要なことである。前述のごとく、製
氷完了寸前においても凝縮能力があり過ぎると、
負荷が軽くなるので、低圧圧力が少なくなり過
ぎ、除氷工程に入つた時の初期のホツトガスの流
量が極めて少なくなり、除氷工程が長くなつた
り、著しい場合は離氷不能となることもあるが、
本考案では、製氷工程の各段階における適正な凝
縮器の能力が得られるので非常にバランスのとれ
た凝縮状態を得ることができる。
次に、第2図〜第7図は本考案による凝縮器の
他の実施例を示すものであり、製氷機構について
は、第1図と同様であるので、同符号を付してそ
の説明は省略するものとする。第2図において
は、冷却フアン15が凝縮パイプ5内、即ち受水
槽14内の水中位置に配設されている。第3図に
示す満水状態では水温は約10℃であり、製氷工程
中で水がある場合には、冷却フアン15により受
水槽14内の水を攪拌すると共に、製氷工程が進
行して徐々に水位が下がり、第4図の製氷中期の
状態となると、水は冷却フアン15によつて凝縮
パイプ5にはねかけられ、あたかもはねかけ式の
凝縮器として作動し、その蒸発潜熱により大きい
凝縮能力を有するもので、この場合、流れ案内体
18の外側より矢印A→B→C→Dの順序で外気
が案内され冷却フアンにより吸入されて凝縮パイ
プ5を冷却する。
更に、製氷完了直前になると、受水槽14内の
水がなくなり、第5図で示す状態となり、凝縮パ
イプ5に付着した水滴も乾燥し、空冷凝縮器とし
て作動している。また、第6図のA,B及び第7
図のA,Bに示す構成は、凝縮器の凝縮能力を更
に向上させるためのもので、コイル状に形成され
た凝縮パイプ5の内側及び外側に長手形状の金属
部材19を取り付けている。該金属部材19は、
ラジエータとして作用し放熱効果を向上させる。
第6図のA,Bの構成では金属部材19が丸棒よ
りなり、第7図のA,Bの構成では金属部材19
が長方形の薄板よりなる。従つて、第6図及び第
7図の構成を用いることにより、前述の凝縮パイ
プ5のみで用いる構成よりも一層冷却効果を向上
させることができる。
Next, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings, in which the same reference numerals indicate the same or corresponding parts. In FIG. 1, what is indicated by numeral 1 is:
This ice-making board is made of a flat plate of copper, aluminum, or the like with good heat conduction, and an evaporator 2 is disposed on the back side of this ice-making board 1. The accumulator 3, compressor 4, condensation pipe 5, dryer 6, and capillary reach tube 7 that constitute the ice making mechanism together with the evaporator 2 are as follows:
As shown in the figure, they are connected in a loop-like closed circuit using a copper pipe (refrigerant pipe) 8. Discharge part 4a of compressor 4
is the suction part 2a of the evaporator 2 via the hot gas valve 9.
It is connected to the. An ice-making water tank 10 is located below the ice-making plate 1.
A circulation pump 11 provided in this ice-making tank 10 is connected to a water sprinkler 12 arranged above the ice-making plate 1.
1, the ice making water tank 10
Ice-making water is continuously supplied to the ice-making plate 1 from the water sprinkler 12.
Supplied on the surface. Water supply valve 13 arranged on the ice-making water tank 10
is connected to the external water supply, and ice making water tank 1
Water can be supplied within 0. Overflowing water from an overflow pipe 10a provided in the ice-making water tank 10 is supplied into a water receiving tank 14 disposed at the lowest position via a hose 10b. This hose 10
Since the amount of water overflowing from b is larger than the amount of water discharged from the drainage part 14a formed in the water receiving tank 14, in the deicing process, the wastewater accumulates in the water receiving tank 14, and the water flowing through the water receiving tank 14
The waste is disposed of outside through an overflow part 14b formed at the top. Further, at a position above the water receiving tank 14, a cooling motor 17 having a cooling fan 15 and an output shaft 16 is installed.
is attached to the ice maker body (not shown). Further, a substantially cylindrical flow guiding body 18 is arranged to surround the condensing pipe 5 in the water receiving tank 14. The flow guide body 18 has an opening 18a at the bottom.
is formed, and a widened part 1 with a flattened top is formed.
8b. In the above configuration, when the air/water cooling combined type condenser according to the present invention is operated, when the ice making mechanism such as the compressor 4 is operated and the ice making process begins, the sprinkling of ice making water from the water sprinkler 12 is started. , ice 1a is gradually formed on ice-making plate 1. When a known ice making thermostat or float switch (not shown) detects that the ice 1a has grown to a predetermined size, the ice making process is switched to the deicing process, the hot gas valve 9 is opened, and the compressor is switched on. By supplying the hot gas No. 4 to the inlet 2a of the evaporator 2, the ice making plate 1 is warmed.
Deicing is performed by slightly melting the contact portion of the ice 1a against the ice 1a. Furthermore, when switching to the deicing process, the water supply valve 13 is opened at the same time as the aforementioned hot gas valve 9 is opened, and ice making water for the next ice making process is supplied into the ice making water tank 10. Water is supplied to the overflow pipe 10a of the ice making water tank 10 and the hose 1
It is sent into the water receiving tank 14 through 0b. The end of the de-icing process can generally be known by detecting the fall of the ice 1a from the ice-making plate 1 or the rise in temperature of the ice-making plate 1 accompanying this fall, and when the de-icing process is completed, By closing the hot gas valve 9 and the water supply valve 13, the cooling fan 15 is rotated to start the next ice making process. In the ice making machine described above, when deicing is completed, the temperature of the evaporator 2 is relatively high, at about 15°C, and the water temperature in the ice making water tank 10 at the beginning of the ice making process from the deicing process is the same as that of the water supply valve. The temperature of the evaporator 2 in the initial state during the ice-making process is also high, and the condensation pressure is also high, as the temperature of the evaporator 2 in the initial state during the ice-making process is also high.
At high pressures of Kg/cm 2 G to 17 Kg/cm 2 G, the compressor 4 will be overloaded and its performance will be significantly impaired. The condenser of the present invention is constructed so that it can perform a sufficient condensing action even under such conditions. Overflowing water flowing down the hose 10b of the ice-making water tank 10 is guided into the water receiving tank 14 and stored therein. In this case, the temperature of the surplus water supplied into the water receiving tank 14 is the same as the temperature of the ice-making residual water in the ice-making water tank 10 (approximately 0
℃), so the water temperature is about 10℃~
The temperature remains relatively low at approximately 15℃. Regarding the water storage status in the water receiving tank 14, the diameter of the drainage part 14a is selected so that the amount of water discharged from the drainage part 14a is sufficiently smaller than the amount of water flowing in from the hose 10b. Even in the open state, water gradually accumulates in the water tank 14, and the water level continues to rise until it reaches the overflow portion 14b. Water is supplied from the water supply valve 13 for the entire period or part of the period during deicing, but the amount of water supplied and the effective volume of the water tank 14 are adjusted so that the water level in the water tank 14 can reach the overflow part 14b during that time. ,
The diameter (that is, the amount of water discharged) of the drainage portion 14a is designed. Therefore, at the start of ice making, the water receiving tank 14 is full of diluted ice water, so the condensation pipe 5
is sufficiently cooled by the cold water as a water-cooled condenser, and has a high condensing capacity. In other words, since the condensing capacity is sufficient during the high load operation at the start of ice making, the pressure does not become high and the load on the compressor 4 is considerably reduced. Furthermore, as the ice-making process continues,
Although the water temperature in the water tank 14 rises, the cooling fan 1
The rotation of 5 promotes evaporation from the water surface,
The latent heat from water evaporation suppresses the rise in water temperature. During this time, water is gradually drained from the drainage part 14a of the water receiving tank 14, and all the water is drained, and the outside air flows from the outside of the guide body 18 as indicated by the arrow A.
The air flows in the order shown by B and C, and the condensing pipe 5 exchanges heat with the outside air. In this case, the water adhering to the wall surface of the water receiving tank 14 and the condensing pipe 5 evaporates, and the condensing pipe 5 is further cooled by the latent heat of vaporization. Thus, in the latter stages of the ice-making process, all the water disappears from the water tank and it becomes dry, operating as a mere air-cooled condenser. This condition is extremely important for the deicing process. As mentioned above, if there is too much condensation capacity even before ice making is complete,
As the load becomes lighter, the low pressure becomes too low, and the initial flow rate of hot gas when the deicing process begins becomes extremely low, which may make the deicing process take longer or, in severe cases, make it impossible to remove the ice. but,
The present invention provides an appropriate condenser capacity at each stage of the ice making process, resulting in a very balanced condensation state. Next, FIGS. 2 to 7 show other embodiments of the condenser according to the present invention, and since the ice making mechanism is the same as that in FIG. It shall be omitted. In FIG. 2, the cooling fan 15 is disposed in the condensing pipe 5, that is, in a submerged position in the water receiving tank 14. In the full water state shown in Fig. 3, the water temperature is approximately 10°C, and if there is water during the ice-making process, the cooling fan 15 stirs the water in the water tank 14, and as the ice-making process progresses, the water temperature gradually increases. When the water level falls and reaches the middle stage of ice making as shown in Fig. 4, the water is splashed onto the condensing pipe 5 by the cooling fan 15, acting as a splash type condenser, and the latent heat of evaporation results in a large amount of condensation. In this case, outside air is guided from the outside of the flow guide body 18 in the order of arrows A→B→C→D and is sucked in by the cooling fan to cool the condensing pipe 5. Furthermore, just before the completion of ice making, the water in the water receiving tank 14 disappears, resulting in the state shown in FIG. 5, and the water droplets adhering to the condensing pipe 5 are also dried, and the condensing pipe 5 is operating as an air-cooled condenser. Also, A, B in Figure 6 and 7
The configurations shown in A and B in the figures are for further improving the condensing capacity of the condenser, and have elongated metal members 19 attached to the inside and outside of the condensing pipe 5 formed in a coil shape. The metal member 19 is
Acts as a radiator and improves heat dissipation effect.
In the configurations A and B in FIG. 6, the metal member 19 is made of a round bar, and in the configurations A and B in FIG.
consists of a rectangular thin plate. Therefore, by using the configurations shown in FIGS. 6 and 7, the cooling effect can be further improved than the configuration using only the condensing pipe 5 described above.
本考案による空水冷兼用型凝縮器は、製氷機構
の製氷用水タンクからの水を受けると共に、排水
を放出するための排水部及び溢水を放出するため
のオーバーフロー部を有する受水槽と、前記製氷
機構の冷媒管に接続され前記受水槽内に配設され
た凝縮パイプと、該凝縮パイプを浸漬するほど前
記受水槽内に水がない場合に同凝縮パイプを空冷
しうる位置に設けられた冷却フアンとを備えてい
るため、次のような効果を奏することができる。
(1) 製氷工程初期は水冷凝縮器として製氷工程後
期は空冷凝縮器として作用し、凝縮器の最適能
力点で作動させることができるので、製氷、除
氷能力共に向上させる事ができる。
(2) 製氷初期の圧縮機の過負荷を防止できる。
(3) 従来無駄に排水されていた冷却水の有効利用
ができる。
(4) 受水槽は毎工程ごとに排水されるので、特別
に洗浄を行わなくてもよく、ゴミ等が付着しな
いので冷却効果の低下を防止できる。
また、本考案の好適な実施例によれば、冷却フ
アンを受水槽内に水没させているため、1個のモ
ータと冷却フアンにより製氷初期の水の攪拌、製
氷途中の水のはねかけを一連の動作で行わせるこ
とができ、製氷工程の各段階に好適に適合した凝
縮器能力が得られる。
更に、受水槽の水の減量時間は、水冷、はねか
け、空冷のタイミングに合わせて穴径(つまり排
水能力)を調節れば、自在に加減することがで
き、製氷機の機能に応じた最適な凝縮能力の特性
が広範囲に得られる。
The air/water cooling type condenser according to the present invention includes a water receiving tank that receives water from an ice making water tank of an ice making mechanism and has a drainage part for discharging waste water and an overflow part for discharging overflow water, and a water receiving tank that receives water from an ice making water tank of an ice making mechanism. a condensing pipe connected to the refrigerant pipe and arranged in the water tank, and a cooling fan installed at a position where the condensing pipe can be air-cooled when there is not enough water in the water tank to submerge the condensing pipe. Because of this, the following effects can be achieved. (1) It functions as a water-cooled condenser during the early stage of the ice-making process and as an air-cooled condenser during the latter stages of the ice-making process, allowing the condenser to operate at its optimum capacity, thereby improving both ice-making and de-icing capabilities. (2) Overload of the compressor at the initial stage of ice making can be prevented. (3) Cooling water, which was previously wasted, can be used effectively. (4) Since the water tank is drained after each process, there is no need for special cleaning, and since no dirt or the like adheres to the water tank, it is possible to prevent the cooling effect from deteriorating. In addition, according to a preferred embodiment of the present invention, the cooling fan is submerged in the water tank, so that a single motor and cooling fan are used to agitate water at the initial stage of ice making and prevent water from splashing during ice making. It can be performed in a series of operations, resulting in a condenser capacity suitably adapted to each stage of the ice-making process. Furthermore, the time required to reduce the amount of water in the water tank can be adjusted freely by adjusting the hole diameter (in other words, the drainage capacity) according to the timing of water cooling, splashing, and air cooling. A wide range of optimum condensing capacity characteristics can be obtained.
第1図は、本考案による空水冷兼用型凝縮器を
備えた製氷機を示す全体構成図、第2図は、本考
案の他の実施例による凝縮器を製氷機に適用した
状態を示す構成図、第3図は、第2図の実施例で
水が満水状態の説明図、第4図は同じく水が減水
した製氷中期の状態の説明図、第5図は、同じく
水が完全になくなつた状態の説明図、第6図の
A,Bは凝縮器パイプの他の実施例を示す斜視図
及び平面図、第7図のA,Bは凝縮パイプの更に
他の実施例を示す平面図及び斜視図である。
5……凝縮パイプ、8……銅管(製氷機構の冷
媒管)、10……製氷用水タンク、14……受水
槽、14a……排水部、14b……オーバーフロ
ー部、15……冷却フアン。
FIG. 1 is an overall configuration diagram showing an ice making machine equipped with an air/water cooling type condenser according to the present invention, and FIG. 2 is a configuration diagram showing a state in which a condenser according to another embodiment of the present invention is applied to the ice making machine. Fig. 3 is an explanatory diagram of the embodiment shown in Fig. 2 when the water is full, Fig. 4 is an explanatory diagram of the state in the middle stage of ice making when the water is reduced, and Fig. 5 is also an explanatory diagram of the state in which the water is completely depleted. An explanatory diagram of the folded state, A and B in Fig. 6 are perspective views and plan views showing another embodiment of the condenser pipe, and A and B in Fig. 7 are plane views showing still another embodiment of the condenser pipe. FIG. 2 is a diagram and a perspective view. 5... Condensing pipe, 8... Copper pipe (refrigerant pipe of ice making mechanism), 10... Water tank for ice making, 14... Water receiving tank, 14a... Drainage section, 14b... Overflow section, 15... Cooling fan.
Claims (1)
ると共に、排水を放出するための排水部14a及
び溢水を放出するためのオーバーフロー部14b
を有する受水槽14と、前記製氷機構の冷媒管に
接続され前記受水槽14内に配設された凝縮パイ
プ5と、該凝縮パイプ5を浸漬するほど前記受水
槽14内に水がない場合に同凝縮パイプ5を空冷
しうる位置に設けられた冷却フアン15とを備え
る空水冷兼用型凝縮器。 A drainage part 14a for receiving water from the ice-making water tank 10 of the ice-making mechanism and for discharging waste water, and an overflow part 14b for discharging overflow water.
a condensing pipe 5 connected to the refrigerant pipe of the ice making mechanism and disposed within the water receiving tank 14; when there is not enough water in the water receiving tank 14 to immerse the condensing pipe 5; An air/water cooling type condenser equipped with a cooling fan 15 provided at a position where the condensing pipe 5 can be air cooled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16579684U JPH0426853Y2 (en) | 1984-11-02 | 1984-11-02 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16579684U JPH0426853Y2 (en) | 1984-11-02 | 1984-11-02 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6181572U JPS6181572U (en) | 1986-05-30 |
| JPH0426853Y2 true JPH0426853Y2 (en) | 1992-06-26 |
Family
ID=30723637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16579684U Expired JPH0426853Y2 (en) | 1984-11-02 | 1984-11-02 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0426853Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5810451B2 (en) * | 2013-12-19 | 2015-11-11 | 村上 輝明 | No wind cooling method |
-
1984
- 1984-11-02 JP JP16579684U patent/JPH0426853Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6181572U (en) | 1986-05-30 |
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