JPH0447583Y2 - - Google Patents

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Publication number
JPH0447583Y2
JPH0447583Y2 JP1987156374U JP15637487U JPH0447583Y2 JP H0447583 Y2 JPH0447583 Y2 JP H0447583Y2 JP 1987156374 U JP1987156374 U JP 1987156374U JP 15637487 U JP15637487 U JP 15637487U JP H0447583 Y2 JPH0447583 Y2 JP H0447583Y2
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JP
Japan
Prior art keywords
solvent
temperature
cooling
expansion valve
refrigerant
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
Application number
JP1987156374U
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Japanese (ja)
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JPH0160171U (en
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Priority to JP1987156374U priority Critical patent/JPH0447583Y2/ja
Publication of JPH0160171U publication Critical patent/JPH0160171U/ja
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Expired legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

【考案の詳細な説明】 (産業上の利用分野) 本考案は、洗浄機の洗浄槽内に発生する白濁を
防止するための洗浄機用溶剤直接冷却装置の改良
に関する。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to an improvement in a solvent direct cooling device for a washing machine to prevent clouding from occurring in a washing tank of a washing machine.

(従来の技術) 洗浄機には、洗浄槽中の溶剤液の昇温を抑制す
るとともに溶剤の蒸発ガスを再液化し、該再液化
により生成された溶剤凝縮液から水分を分離する
ための溶剤冷却装置が不可欠の手段として備えら
れている。該冷却装置としては、従来、冷却した
フロンを冷媒として循環させることにより上述し
た溶剤液の昇温抑制、溶剤蒸発ガスの再液化およ
び溶剤凝縮液の水分離を行う洗浄機用溶剤直接冷
却装置が用いられている。
(Prior art) A cleaning machine is equipped with a solvent that suppresses the temperature rise of the solvent solution in the cleaning tank, re-liquefies the evaporated gas of the solvent, and separates moisture from the solvent condensate produced by the re-liquefaction. Cooling equipment is provided as an essential measure. Conventionally, such cooling devices include direct solvent cooling devices for washing machines that suppress the temperature increase of the solvent liquid, reliquefy the evaporated solvent gas, and separate water from the solvent condensate by circulating cooled Freon as a refrigerant. It is used.

第2図は従来の洗浄機用溶剤直接冷却装置の構
成図であつて、冷凍機1で生成された高圧冷媒液
L1は、膨張弁V2によつて低圧低温溶剤液L2
になり、また膨張弁V3によつて低圧低温冷媒液
L3になる。低圧低温冷媒液L2は、溶剤蒸発ガ
ス冷却器2で溶剤蒸発ガスYGを冷却して再液化
することにより溶剤凝縮液YCとするとともに低
圧低温冷媒液L4となる。低圧低温冷媒液L4
は、溶剤凝縮液水分離器14の水分離用冷却器4
に入り溶剤凝縮液YCを冷却することによつて溶
剤凝縮液YC中の水分を析出させる。低圧低温冷
媒液L4は、上記の水分離用冷却器4における熱
交換によつて冷媒蒸発ガスGとなり冷凍機1へ戻
る。
FIG. 2 is a block diagram of a conventional solvent direct cooling device for a washing machine, in which a high-pressure refrigerant liquid L1 generated in a refrigerator 1 is transferred to a low-pressure low-temperature solvent liquid L2 by an expansion valve V2.
It also becomes a low-pressure low-temperature refrigerant liquid L3 by the expansion valve V3. The low-pressure low-temperature refrigerant liquid L2 is turned into a solvent condensate YC by cooling and re-liquefying the solvent evaporated gas YG in the solvent evaporative gas cooler 2, and also becomes a low-pressure low-temperature refrigerant liquid L4. Low pressure low temperature refrigerant liquid L4
is the water separation cooler 4 of the solvent condensate water separator 14
The water in the solvent condensate YC is precipitated by cooling the solvent condensate YC. The low-pressure low-temperature refrigerant liquid L4 becomes refrigerant evaporated gas G through heat exchange in the water separation cooler 4 and returns to the refrigerator 1.

低圧低温冷媒液L3は、溶剤液冷却槽12の溶
剤液冷却器3に入り、溶剤液と熱交換することに
よつて該溶剤液を冷却して冷媒蒸発ガスGとなり
冷凍機1へ戻る。以上の冷媒循環経路における膨
張弁V2とV3の調節は、冷媒蒸発ガスGの温度
に基づいて行われる。洗浄槽11において被洗浄
物10を洗浄する溶剤液はオーバーフローして蒸
気槽13に入り、ここで加熱されることにより蒸
発して溶剤蒸発ガスYGとなる。該溶剤蒸発ガス
YGは、前述した溶剤蒸発ガス冷却器2によつて
低圧低温冷媒液L2と熱交換することにより再液
化され、溶剤凝縮液YCとなつて溶剤凝縮液水分
離器14に集められる。溶剤凝縮液YCは、前述
した水分離用冷却器4によつて低圧低温冷媒液L
4と熱交換することにより水分を析出してこれを
分離され、戻り溶剤液YRとなつて溶剤液冷却槽
12に戻る。溶剤液冷却槽12は、戻り溶剤液
YRを受入れることによつて増量する溶剤をオー
バフローさせることにより、オーバフロー溶剤液
YFとして洗浄槽11へ送出する。該オーバフロ
ー溶剤液YFは、前述した溶剤液冷却器3による
低圧低温冷媒液L3との熱交換によつて冷却され
ているので、洗浄槽11中の溶剤液の昇温を抑制
することになる。
The low-pressure low-temperature refrigerant liquid L3 enters the solvent liquid cooler 3 of the solvent liquid cooling tank 12, cools the solvent liquid by exchanging heat with the solvent liquid, and returns to the refrigerator 1 as a refrigerant evaporated gas G. The above-mentioned adjustment of the expansion valves V2 and V3 in the refrigerant circulation path is performed based on the temperature of the refrigerant evaporated gas G. The solvent solution for cleaning the object to be cleaned 10 in the cleaning tank 11 overflows and enters the steam tank 13, where it is heated and evaporated to become solvent evaporation gas YG. The solvent evaporation gas
YG is reliquefied by exchanging heat with the low-pressure low-temperature refrigerant liquid L2 by the above-mentioned solvent evaporative gas cooler 2, and is collected in the solvent condensate water separator 14 as a solvent condensate YC. The solvent condensate YC is converted into a low-pressure low-temperature refrigerant liquid L by the water separation cooler 4 described above.
By exchanging heat with 4, moisture is precipitated and separated, and returned to the solvent liquid cooling tank 12 as returned solvent liquid YR. The solvent liquid cooling tank 12 is a returning solvent liquid.
Overflow solvent solution by overflowing the solvent which increases by accepting YR
It is sent to the cleaning tank 11 as YF. Since the overflow solvent liquid YF is cooled by heat exchange with the low-pressure low-temperature refrigerant liquid L3 by the above-mentioned solvent liquid cooler 3, the temperature increase of the solvent liquid in the cleaning tank 11 is suppressed.

(考案が解決しようとする問題点) 上述した従来の洗浄機用溶剤直接冷却装置で
は、溶剤として高沸点のものを用いる場合、冷却
能力を高める必要があるため溶剤液冷却器3およ
び水分離用冷却器4に流入する冷媒液が5℃程度
にまで下がる。一方、沸点の高い溶剤、たとえば
トリクロルエチレンは、30℃おいて0.04%程度溶
け込ませ得る水分を5℃においては0.014%程度
しか溶け込ませられない。
(Problems to be solved by the invention) In the conventional solvent direct cooling device for washing machines described above, when a high boiling point solvent is used, it is necessary to increase the cooling capacity. The temperature of the refrigerant liquid flowing into the cooler 4 drops to about 5°C. On the other hand, a solvent with a high boiling point, such as trichlorethylene, can dissolve about 0.04% water at 30°C, but only about 0.014% at 5°C.

したがつて、30℃の溶剤凝縮液YCが水分離用
冷却器4による熱交換で5℃までその液温を下げ
ると約0.026%の水分が析出するが、この析出水
分の全量を溶剤凝縮液水分離器14の能力で分離
することが困難であるため、残存する水分が溶剤
凝縮液水分離器14中の溶剤凝縮液と混在し、該
溶剤凝縮液を白濁させる。この白濁は、戻り溶剤
液YRによつて溶剤液冷却槽12に持込まれる。
Therefore, when the solvent condensate YC at 30°C is lowered to 5°C by heat exchange with the water separation cooler 4, approximately 0.026% water will precipitate, but the entire amount of this precipitated water will be absorbed into the solvent condensate. Since it is difficult to separate with the capacity of the water separator 14, the remaining moisture mixes with the solvent condensate in the solvent condensate water separator 14, making the solvent condensate cloudy. This cloudiness is carried into the solvent liquid cooling tank 12 by the returned solvent liquid YR.

また溶剤液冷却槽12において溶剤凝縮液水分
離器14における上述の現象が起きると、約
0.026%の析出水分が溶剤液と混在して該溶剤液
の白濁を生じる。以上の2箇所で生じた白濁は、
オーバフロー溶剤液YFによつて洗浄槽11にも
たらされ、被洗浄物10の洗浄中の状態を見えな
くするとともに白濁を形成する上述の水分が被洗
浄物10の表面に微粒痕を発生させることにより
目的とする清浄な面を得られなくするという問題
を生ずる。
Furthermore, when the above-mentioned phenomenon occurs in the solvent condensate water separator 14 in the solvent liquid cooling tank 12, approximately
The precipitated water of 0.026% mixes with the solvent solution, causing the solvent solution to become cloudy. The cloudiness that occurs in the above two places is
The above-mentioned water, which is brought into the cleaning tank 11 by the overflow solvent liquid YF and which makes the state of the object 10 being cleaned invisible and forms cloudiness, generates fine particle marks on the surface of the object 10 to be cleaned. This causes the problem that the desired clean surface cannot be obtained.

本考案の目的は、溶剤の循環がもつとも捕えら
れ易い溶剤蒸発ガスの温度を計測し、該計測値に
基づいて冷却能力の調整を行い、水分離用冷却器
および溶剤液冷却器における溶剤と冷媒との温度
差を、溶剤の冷却を大きく妨げない範囲でできる
だけ少なくすることにより、溶剤からの水分析出
を抑制して溶剤中の白濁の発生を防止する洗浄機
用白濁防止型溶剤直接冷却装置を提供することで
ある。
The purpose of this invention is to measure the temperature of solvent evaporation gas that is easily captured during solvent circulation, and to adjust the cooling capacity based on the measured value. Anti-clouding solvent direct cooling device for washing machines that suppresses water analysis from the solvent and prevents clouding in the solvent by minimizing the temperature difference between the The goal is to provide the following.

(問題点を解決するための手段) 本考案は、上記の目的を達成するために次の手
段構成を有する。すなわち、本考案の洗浄機用白
濁防止型溶剤直接冷却装置は、洗浄機用の溶剤を
冷却する直接冷却装置において、溶剤蒸発ガスの
温度を測定するための溶剤蒸発ガス温度センサ
と; 冷媒蒸発ガスの温度を測定するための冷媒
蒸発ガス温度センサと; 前記2つの温度センサ
からの温度データを受けて、洗浄機の運転開始時
には、溶剤蒸発ガス温度が予め設定した温度に達
するまでは、主電源オンオフ制御の冷却装置にあ
つては主電源をオフにしておき、また膨張弁制御
の冷却装置にあつては冷却能力を抑制するように
膨張弁の開度を設定しておき、溶剤蒸発ガス温度
が予め設定した温度に達した後は冷却装置を通常
に稼働させるが、溶剤蒸発ガスの温度と冷媒蒸発
ガスの温度との差が水分析出量に基づいて予め定
めた値を越えると主電源オンオフ制御の冷却装置
にあつては主電源をオフにし、また膨張弁制御の
冷却装置にあつては冷却能力を抑制するように膨
張弁の開度を設定し、温度差が前記予め定めた値
以下になると、それぞれ、主電源をオンにする
か、通常の冷却能力を発揮するように膨張弁の開
度を設定する制御を行う冷却能力制御部と;を具
備することを特徴とする洗浄機用白濁防止型溶剤
直接冷却装置である。
(Means for solving the problems) The present invention has the following means configuration to achieve the above object. That is, the clouding prevention type solvent direct cooling device for a washing machine of the present invention is a direct cooling device for cooling a solvent for a washing machine, and includes a solvent evaporation gas temperature sensor for measuring the temperature of the solvent evaporation gas; a refrigerant evaporated gas temperature sensor for measuring the temperature of the solvent; upon receiving the temperature data from the two temperature sensors, when the washer starts operating, the main power supply is turned off until the solvent evaporated gas temperature reaches a preset temperature; For cooling systems with on-off control, the main power is turned off, and for cooling systems with expansion valve control, the opening degree of the expansion valve is set to suppress the cooling capacity, and the temperature of the solvent evaporated gas is After reaching the preset temperature, the cooling system will operate normally, but if the difference between the temperature of the solvent evaporated gas and the temperature of the refrigerant evaporated gas exceeds a predetermined value based on the water analysis output amount, the main power will be turned off. In the case of an on-off control cooling device, the main power is turned off, and in the case of an expansion valve control cooling device, the opening degree of the expansion valve is set to suppress the cooling capacity, and the temperature difference is set to the predetermined value. A washing machine characterized by comprising: a cooling capacity control unit that controls to turn on the main power or set the opening degree of the expansion valve so that the normal cooling capacity is exhibited when the following conditions are reached: This is a direct cooling device for solvents that prevents clouding.

(作用) 以下、上記の手段構成を有する洗浄機用白濁防止
型溶剤直接冷却装置の作用について説明する。
(Function) Hereinafter, the function of the clouding prevention type solvent direct cooling device for a washing machine having the above-mentioned means configuration will be explained.

本考案の白濁防止型洗浄機用溶剤直接冷却装置
は、溶剤の蒸発ガス温度を計測する溶剤蒸発ガス
温度センサを有しており、その計測値は冷却能力
を調節する冷却能力制御部へ送出される。
The clouding prevention type solvent direct cooling device for washing machines of the present invention has a solvent evaporative gas temperature sensor that measures the temperature of the evaporative gas of the solvent, and the measured value is sent to the cooling capacity control unit that adjusts the cooling capacity. Ru.

冷却能力の制御は、冷却装置の主電源を切・断
する場合と、運転中の冷却装置において低温の冷
媒液を生成する膨張弁の開度を調整することによ
り、上記低温の冷媒液の温度および流量を定める
場合とがある。
The cooling capacity can be controlled by controlling the temperature of the low-temperature refrigerant liquid by turning off or disconnecting the main power supply of the cooling system, and by adjusting the opening degree of the expansion valve that generates the low-temperature refrigerant liquid in the operating cooling system. and the flow rate may be determined.

前者の場合には、洗浄機の運転開始と同時には
冷却装置を稼働させず、上記の溶剤蒸発ガス温度
センサの計測値が所定の値に達した時冷却能力制
御部が冷却装置を稼働させて冷媒を循環させる。
In the former case, the cooling device is not operated at the same time as the washer starts operating, but the cooling capacity control unit operates the cooling device when the measured value of the solvent evaporative gas temperature sensor reaches a predetermined value. Circulate the refrigerant.

したがつて、溶剤凝縮液水分離器の水分離用冷
却器および溶剤液冷却槽の溶剤液冷却器が溶剤の
昇温後徐々に低温になつて行き、溶剤と冷媒との
温度差が大きい急激な冷却を行わないので、溶剤
からの水分の析出が抑制できる。
Therefore, the water separation cooler of the solvent condensate water separator and the solvent liquid cooler of the solvent liquid cooling tank gradually become low temperature after the temperature of the solvent is raised, and the temperature difference between the solvent and refrigerant is large and the temperature difference between the solvent and the refrigerant is large. Since no significant cooling is performed, precipitation of moisture from the solvent can be suppressed.

また冷却装置が稼働を始めた後には、冷却能力
制御部が溶剤蒸発ガス温度センサの計測値と併せ
て該冷却装置運転のために計測している冷媒蒸発
ガス温度の値を把握し、これらの値の差が所定の
値を越えると冷却装置を停止させ、所定の値以下
になると冷却装置を稼働させる。したがつて、溶
剤凝縮液水分離器および溶剤液冷却槽における溶
剤と冷媒の温度差を溶剤の冷却を妨げない範囲で
小さくすることができ、溶剤からの水分の析出を
抑制することができる。
In addition, after the cooling device starts operating, the cooling capacity control unit grasps the value of the refrigerant evaporative gas temperature measured for the cooling device operation together with the measured value of the solvent evaporative gas temperature sensor, and When the difference in values exceeds a predetermined value, the cooling device is stopped, and when the difference falls below a predetermined value, the cooling device is activated. Therefore, the temperature difference between the solvent and the refrigerant in the solvent condensate water separator and the solvent liquid cooling tank can be reduced within a range that does not impede cooling of the solvent, and precipitation of moisture from the solvent can be suppressed.

後者の場合には、冷却能力制御部が前述した膨
張弁の開度を調節するが、洗浄機の運転を開始す
る時には溶剤蒸発ガス温度センサの計測値が所定
の値に達するまで冷却能力を抑制するように該膨
張弁の開度を設定する。冷却装置が通常の冷却能
力を発揮した後には、上述した冷媒蒸発ガス温度
の計測値と溶剤蒸発ガス温度センサの計測値との
差が所定の値を越えると冷却能力を抑制するよう
に膨張弁の開度を設定し、所定の値以下になると
通常の冷却能力を発揮するように膨張弁の開度を
設定する。したがつて、洗浄機の運転を開始する
時の溶剤の急冷および溶剤と冷媒との温度差が大
きいままでの溶剤冷却が行われないので、溶剤か
らの水分の析出が抑制できる。
In the latter case, the cooling capacity control unit adjusts the opening degree of the expansion valve described above, but when the washer starts operating, the cooling capacity is suppressed until the measured value of the solvent evaporation gas temperature sensor reaches a predetermined value. The opening degree of the expansion valve is set so that After the cooling device exhibits its normal cooling capacity, an expansion valve is installed to suppress the cooling capacity when the difference between the measured value of the refrigerant evaporative gas temperature and the measured value of the solvent evaporative gas temperature sensor exceeds a predetermined value. The opening degree of the expansion valve is set so that the normal cooling capacity is exhibited when the opening degree becomes below a predetermined value. Therefore, since the solvent is not rapidly cooled when the washing machine starts operating, and the solvent is not cooled while the temperature difference between the solvent and the refrigerant remains large, precipitation of moisture from the solvent can be suppressed.

以上説明したように、本考案の洗浄機用白濁防
止型溶剤直接冷却装置は、溶媒蒸発ガス温度セン
サの計測値に基づき冷却能力制御部が冷却装置の
稼働・停止または低温の冷媒液を生成する膨張弁
の開度調整を指令することにより、溶剤と冷媒と
の間に過大な温度差が生じないように冷却能力を
調節するので、溶剤中の水分析出が抑制され該水
分の析出による洗浄槽中の白濁を防止できる。
As explained above, in the anti-clouding solvent direct cooling device for washing machines of the present invention, the cooling capacity control section operates/stops the cooling device or generates a low-temperature refrigerant liquid based on the measured value of the solvent evaporation gas temperature sensor. By commanding the opening degree of the expansion valve, the cooling capacity is adjusted so that an excessive temperature difference does not occur between the solvent and the refrigerant, which suppresses the separation of water in the solvent and prevents cleaning due to the precipitation of water. Can prevent cloudiness in the tank.

(実施例) 以下、本考案の洗浄機用白濁防止型溶剤直接冷
却装置の実施例について図面を用いて説明する。
(Example) Hereinafter, an example of the anti-clouding solvent direct cooling device for a washing machine according to the present invention will be described with reference to the drawings.

第1図は本考案実施例の洗浄機用白濁防止型溶
剤直接冷却装置の構成図であつて、同図のaは、
冷却能力制御部が冷却装置を構成する冷凍機の稼
働・停止を指令することにより該冷却装置の冷却
能力を調節する構成例であり、同図のbは、冷却
能力制御部が冷却装置を構成する膨張弁の開度設
定を指令することにより該冷却装置の冷却能力を
調節する構成例である。
FIG. 1 is a block diagram of a clouding prevention type solvent direct cooling device for a washing machine according to an embodiment of the present invention, and a in the figure is a
This is an example of a configuration in which the cooling capacity control section adjusts the cooling capacity of the cooling device by instructing the operation/stop of the refrigerator that constitutes the cooling device. This is a configuration example in which the cooling capacity of the cooling device is adjusted by commanding the opening degree setting of the expansion valve.

上記のaでは、冷凍機1が生成する高圧冷媒液
L1が膨張弁V2により低圧低温冷媒液L2とな
つて溶剤蒸発ガス冷却器2へ流入し、膨張弁V3
により低圧低温冷媒液L3となつて溶剤液冷却器
3へ流入する。溶剤蒸発ガス冷却器2から流出す
る低圧低温冷媒液L4は、溶剤蒸発ガス冷却器2
によつて再液化された溶剤凝縮液中の水分を分離
する溶剤凝縮液水分離器14の水分離用冷却器4
において冷媒蒸発ガスGとなる。該冷媒蒸発ガス
Gは、溶剤液冷却器3において低圧低温冷媒液L
3が変態した冷媒蒸発ガスGと合体して冷凍機1
へ戻る。溶剤蒸発ガス温度センサ2Tの計測値は
冷凍機1に設けた開閉器制御盤1CSに入り、洗
浄機の運転を開始する時には、上記の計測値が所
定の値に達した時開閉器制御盤1CSが開閉器1
Sに閉を指令することにより冷凍機主電源1Pを
冷凍機1に接続させて冷凍機1を稼働させる。
In a above, the high-pressure refrigerant liquid L1 generated by the refrigerator 1 becomes the low-pressure low-temperature refrigerant liquid L2 by the expansion valve V2 and flows into the solvent evaporative gas cooler 2, and the expansion valve V3
As a result, it becomes a low-pressure low-temperature refrigerant liquid L3 and flows into the solvent liquid cooler 3. The low-pressure low-temperature refrigerant liquid L4 flowing out from the solvent evaporative gas cooler 2 is transferred to the solvent evaporative gas cooler 2.
The water separation cooler 4 of the solvent condensate water separator 14 that separates water in the solvent condensate re-liquefied by
The refrigerant becomes evaporated gas G. The refrigerant evaporated gas G is converted into a low-pressure low-temperature refrigerant liquid L in the solvent liquid cooler 3.
3 is combined with the transformed refrigerant evaporated gas G to form refrigerator 1.
Return to The measured value of the solvent evaporative gas temperature sensor 2T is entered into the switch control panel 1CS installed in the refrigerator 1, and when the above measurement value reaches a predetermined value, the switch control panel 1CS is sent to start operation of the washing machine. is switch 1
By instructing S to close, the main power source 1P of the refrigerator is connected to the refrigerator 1, and the refrigerator 1 is operated.

また冷凍機1が稼働を始めた後には、開閉器制
御盤1CSが溶剤蒸発ガス温度センサ2Tの計測
値と併せて冷媒蒸発ガス温度の計測値を把握し、
上記両計測値の差が所定の値を越えると、開閉器
1Sに開を指令することにより冷凍機主電源1P
を冷凍機1から切り放させて冷凍機1を停止させ
る。上記両計測値の差が所定の値以下になると開
閉器1Sに閉を指令することにより冷凍機主電源
1Pを冷凍機1に接続させて冷凍機1を稼働させ
る。
Furthermore, after the refrigerator 1 starts operating, the switch control panel 1CS grasps the measured value of the refrigerant evaporative gas temperature together with the measured value of the solvent evaporative gas temperature sensor 2T,
When the difference between the above two measured values exceeds a predetermined value, the refrigerator main power supply 1P is commanded to open the switch 1S.
is disconnected from the refrigerator 1 to stop the refrigerator 1. When the difference between the two measured values becomes equal to or less than a predetermined value, the main power source 1P of the refrigerator is connected to the refrigerator 1 to operate the refrigerator 1 by instructing the switch 1S to close.

第1図のbでは、溶剤蒸発ガス温度センサ2T
の計測値を膨張弁制御盤1CVが取込み、該膨張
弁制御盤1CVは、上記の計測値および上記の計
測値と冷媒蒸発ガス温度の計測値との差のそれぞ
れに基づいた膨張弁V2の開度を設定する指令を
膨張弁開度設定用モータ1Mへ送出する。
In Fig. 1b, the solvent evaporated gas temperature sensor 2T
The expansion valve control board 1CV takes in the measured value of , and the expansion valve control board 1CV controls the opening of the expansion valve V2 based on the above measured value and the difference between the above measured value and the measured value of the refrigerant evaporated gas temperature. A command for setting the opening degree is sent to the expansion valve opening degree setting motor 1M.

膨張弁開度設定用モータ1Mは、上記の指令を
受けて膨張弁開度設定軸1Rを回転させ、膨張弁
V2の開度を膨張弁制御盤1CVの指令する値に
設定する。洗浄機が運転を開始する時に膨張弁制
御盤1CVが指令する膨張弁開度の設定値は、溶
剤蒸発ガス温度センサの計測値が所定の値に達す
るまでは抑制した冷却能力しか有しない低圧低温
冷媒液L2を生成する開度値であり、上記の計測
値が所定の値に達した時には通常の能力を発揮す
る低圧低温冷媒液L2を生成する開度値である。
The expansion valve opening setting motor 1M rotates the expansion valve opening setting shaft 1R in response to the above command, and sets the opening of the expansion valve V2 to a value commanded by the expansion valve control panel 1CV. The set value of the expansion valve opening commanded by the expansion valve control panel 1CV when the washer starts operation is a low-pressure, low-temperature setting that only has a suppressed cooling capacity until the measured value of the solvent evaporation gas temperature sensor reaches a predetermined value. This is the opening degree value that generates the refrigerant liquid L2, and is the opening degree value that generates the low-pressure low-temperature refrigerant liquid L2 that exhibits normal performance when the above measured value reaches a predetermined value.

また冷却装置が通常の冷却能力を発揮した後に
は、膨張弁制御盤1CVが指令する膨張弁開度の
設定値は、溶剤蒸発ガス温度センサの計測値と冷
媒蒸発ガス温度の計測値の差が所定の値を越える
時は抑制した冷却能力した有しない低圧低温冷媒
液L2を生成する開度値であり、上記の差が所定
の値以下になる時は通常の冷却能力を発揮する低
圧低温冷媒液L2を生成する開度値である。
In addition, after the cooling system has achieved its normal cooling capacity, the expansion valve opening setting commanded by the expansion valve control panel 1CV is determined by the difference between the measured value of the solvent evaporative gas temperature sensor and the measured value of the refrigerant evaporative gas temperature. When it exceeds a predetermined value, it is an opening value that produces a low-pressure low-temperature refrigerant liquid L2 that does not have the suppressed cooling ability, and when the above difference is less than a predetermined value, it is a low-pressure low-temperature refrigerant that exhibits a normal cooling ability. This is the opening degree value that generates the liquid L2.

(考案の効果) 以上説明したように、本考案の洗浄機用白濁防
止型溶剤直接冷却装置は、溶剤蒸発ガス温度セン
サの計測値に基づき冷却能力制御部が冷却装置の
稼働・停止または低温の冷媒液を生成する膨張弁
の開度調整を指令することにより、溶剤と冷媒と
の間に過大な温度差が生じないように冷却能力を
調節する。したがつて、溶剤中の水分析出が抑制
され該水分の析出による洗浄槽中の白濁が防止で
きる本考案の白濁防止型洗浄機用溶剤直接冷却装
置を設けた洗浄機は、高沸点溶剤を用いる場合も
被洗浄物の洗浄中の状態が明視できるとともに、
被洗浄物表面から水分の微粒痕をほとんど無くせ
るため目的とする清浄な面が得やすいという利点
を有する。
(Effects of the invention) As explained above, in the anti-clouding solvent direct cooling device for washing machines of the present invention, the cooling capacity control section controls whether the cooling device starts or stops or changes to low temperature based on the measured value of the solvent evaporation gas temperature sensor. By commanding the opening degree adjustment of the expansion valve that generates the refrigerant liquid, the cooling capacity is adjusted so that an excessive temperature difference does not occur between the solvent and the refrigerant. Therefore, the washing machine equipped with the clouding prevention type solvent direct cooling device for washing machines of the present invention, which suppresses the water analysis and precipitation in the solvent and prevents clouding in the washing tank due to the precipitation of water, does not require high boiling point solvents. When using it, you can clearly see the condition of the object being cleaned, and
This method has the advantage that it is easy to obtain the desired clean surface because traces of moisture particles can be almost completely eliminated from the surface of the object to be cleaned.

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

第1図は本考案実施例の洗浄機用白濁防止型溶
剤直接冷却装置の構成図、第2図は従来の洗浄機
用溶剤直接冷却装置の構成図である。 1……冷凍機、1CS……開閉器制御盤、1CV
……膨張弁制御盤、1M……膨張弁開度設定用モ
ータ、1P……冷凍器主電源、1R……膨張弁開
度設定軸、1S……開閉器、2……溶剤蒸発ガス
冷却器、2T……溶剤蒸発ガス温度センサ、3…
…溶剤液冷却器、4……水分離用冷却器、10…
…被洗浄物、11……洗浄槽、12……溶剤液冷
却槽、13……蒸気槽、14……溶剤凝縮液水分
離器、G……冷媒蒸発ガス、L1……高圧冷媒
液、L2,L3,L4……低圧低温冷媒液、V
2,V3……膨張弁、YC……溶剤凝縮液、YF…
…オーバフロー溶剤液、YG……溶剤蒸発ガス、
YR……戻り溶剤液。
FIG. 1 is a block diagram of an anti-clouding type solvent direct cooling device for a washing machine according to an embodiment of the present invention, and FIG. 2 is a block diagram of a conventional solvent direct cooling device for a washing machine. 1... Refrigerator, 1CS... Switch control panel, 1CV
...Expansion valve control panel, 1M...Expansion valve opening setting motor, 1P...Freezer main power supply, 1R...Expansion valve opening setting axis, 1S...Switch switch, 2...Solvent evaporative gas cooler , 2T...Solvent evaporation gas temperature sensor, 3...
...Solvent liquid cooler, 4...Water separation cooler, 10...
...Object to be cleaned, 11...Cleaning tank, 12...Solvent liquid cooling tank, 13...Steam tank, 14...Solvent condensate water separator, G...Refrigerant evaporation gas, L1...High pressure refrigerant liquid, L2 , L3, L4...Low pressure low temperature refrigerant liquid, V
2, V3...Expansion valve, YC...Solvent condensate, YF...
...Overflow solvent liquid, YG...Solvent evaporation gas,
YR... Return solvent liquid.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 洗浄機用の溶剤を冷却する直接冷却装置におい
て、溶剤蒸発ガスの温度を測定するための溶剤蒸
発ガス温度センサと; 冷媒蒸発ガスの温度を測
定するための冷媒蒸発ガス温度センサと; 前記
2つの温度センサからの温度データを受けて、洗
浄機の運転開始時には、溶剤蒸発ガス温度が予め
設定した温度に達するまでは、主電源オンオフ制
御の冷却装置にあつては主電源をオフにしてお
き、また膨張弁制御の冷却装置にあつては冷却能
力を抑制するように膨張弁の開度を設定してお
き、溶剤蒸発ガス温度が予め設定した温度に達し
た後は冷却装置を通常に稼働させるが、溶剤蒸発
ガスの温度と冷媒蒸発ガスの温度との差が水分析
出量に基づいて予め定めた値を越えると主電源オ
ンオフ制御の冷却装置にあつては主電源をオフに
し、また膨張弁制御の冷却装置にあつては冷却能
力を抑制するように膨張弁の開度を設定し、温度
差が前記予め定めた値以下になると、それぞれ、
主電源をオンにするか、通常の冷却能力を発揮す
るように膨張弁の開度を設定する制御を行う冷却
能力制御部と; を具備することを特徴とする洗
浄機用白濁防止型溶剤直接冷却装置。
In a direct cooling device for cooling a solvent for a washing machine, a solvent evaporative gas temperature sensor for measuring the temperature of the solvent evaporative gas; a refrigerant evaporative gas temperature sensor for measuring the temperature of the refrigerant evaporative gas; Upon receiving the temperature data from the temperature sensor, when the washer starts operating, the main power is turned off in the case of a cooling device with main power on/off control until the solvent evaporated gas temperature reaches a preset temperature. In the case of an expansion valve-controlled cooling system, the opening degree of the expansion valve is set to suppress the cooling capacity, and the cooling system is operated normally after the solvent evaporated gas temperature reaches a preset temperature. However, if the difference between the temperature of the solvent evaporation gas and the temperature of the refrigerant evaporation gas exceeds a predetermined value based on the amount of water analyzed, the main power is turned off in the case of a cooling system with main power on/off control, and the expansion is stopped. In the case of a valve-controlled cooling device, the opening degree of the expansion valve is set to suppress the cooling capacity, and when the temperature difference becomes less than the predetermined value,
A cooling capacity control unit that controls turning on the main power supply or setting the opening degree of an expansion valve so as to exhibit normal cooling capacity; Cooling system.
JP1987156374U 1987-10-13 1987-10-13 Expired JPH0447583Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987156374U JPH0447583Y2 (en) 1987-10-13 1987-10-13

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987156374U JPH0447583Y2 (en) 1987-10-13 1987-10-13

Publications (2)

Publication Number Publication Date
JPH0160171U JPH0160171U (en) 1989-04-17
JPH0447583Y2 true JPH0447583Y2 (en) 1992-11-10

Family

ID=31434857

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987156374U Expired JPH0447583Y2 (en) 1987-10-13 1987-10-13

Country Status (1)

Country Link
JP (1) JPH0447583Y2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5140646A (en) * 1974-10-04 1976-04-05 Fujikura Ltd REITOSOCHI
JPS54156253A (en) * 1978-05-29 1979-12-10 Sanyo Electric Co Ltd Freezer controller
DE2966548D1 (en) * 1978-06-28 1984-02-23 James W Mccord Vapor generating and recovering apparatus

Also Published As

Publication number Publication date
JPH0160171U (en) 1989-04-17

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