JP2634232B2 - Dry cleaning machine - Google Patents
Dry cleaning machineInfo
- Publication number
- JP2634232B2 JP2634232B2 JP1072833A JP7283389A JP2634232B2 JP 2634232 B2 JP2634232 B2 JP 2634232B2 JP 1072833 A JP1072833 A JP 1072833A JP 7283389 A JP7283389 A JP 7283389A JP 2634232 B2 JP2634232 B2 JP 2634232B2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- concentration
- ultrasonic
- cleaning machine
- dry cleaning
- 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 - Fee Related
Links
- 238000005108 dry cleaning Methods 0.000 title claims description 21
- 239000002904 solvent Substances 0.000 claims description 97
- 238000009835 boiling Methods 0.000 claims description 39
- 238000005259 measurement Methods 0.000 claims description 20
- 238000012545 processing Methods 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 11
- 230000010355 oscillation Effects 0.000 claims description 8
- 238000001514 detection method Methods 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 7
- 238000004821 distillation Methods 0.000 claims description 4
- 230000010356 wave oscillation Effects 0.000 claims description 2
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 7
- 229950011008 tetrachloroethylene Drugs 0.000 description 7
- 230000005856 abnormality Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000010354 integration Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000001902 propagating effect Effects 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 235000007586 terpenes Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 210000002268 wool Anatomy 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000007274 generation of a signal involved in cell-cell signaling Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
Landscapes
- Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (AREA)
- Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は溶剤の濃度監視を行うドライクリーニング機
械に関するものである。Description: TECHNICAL FIELD The present invention relates to a dry cleaning machine for monitoring the concentration of a solvent.
(従来の技術) 第4図は相溶性二成分溶剤を使用する従来のドライク
リーナの溶剤管理装置の1例を示す。第5図は第4図に
示すドライクリーナを溶剤置換型に使用した場合の乾燥
時間短縮の効果を示す例である。(Prior Art) FIG. 4 shows an example of a conventional dry cleaner solvent management apparatus using a compatible binary solvent. FIG. 5 is an example showing the effect of shortening the drying time when the dry cleaner shown in FIG. 4 is used in a solvent replacement type.
さて第4図は高沸点溶剤であるターペン、パークロル
エチレン及び比較的高沸点溶剤である1.1.1トリクロル
エタン等の単一溶剤専用ドライクリーナに、R113,R11な
どの低沸点溶剤タンク、同溶剤を処理槽へ供給するため
の機能、及び高沸点溶剤と低沸点溶剤の混合液を分留再
生するための機能を付加し、洗浄の途中又は乾燥の直前
で高沸点溶剤から互いに溶解性を有する低沸点溶剤に切
替えることにより、乾燥時間を半減するようにしたドラ
イクリーナの1例である。Fig. 4 shows a dry cleaner for a single solvent such as terpen, perchlorethylene, which is a high boiling solvent, and 1.1.1 trichloroethane, which is a relatively high boiling solvent, a low boiling solvent tank such as R113, R11, etc. To the treatment tank, and a function to fractionate and regenerate a mixed solution of a high-boiling solvent and a low-boiling solvent, and have mutual solubility from the high-boiling solvent during washing or immediately before drying. This is an example of a dry cleaner in which the drying time is reduced to half by switching to a low boiling point solvent.
次に第4図において、第1の溶剤4を低沸点溶剤、第
2の溶剤4aを高沸点溶剤と仮定して、洗浄の途中で高沸
点溶剤4aと低沸点溶剤4を入替える方法を説明する。Next, in FIG. 4, assuming that the first solvent 4 is a low boiling solvent and the second solvent 4a is a high boiling solvent, a method of exchanging the high boiling solvent 4a and the low boiling solvent 4 during the washing will be described. I do.
.タンク3aから高沸点溶剤4aをバルブ5aを介してポン
プ6により汲み揚げ、バルブ7、フィルタ8、又はバル
ブ9の経路で処理槽10に必要量を送り込む。. The high-boiling solvent 4a is pumped from the tank 3a by the pump 6 via the valve 5a, and the required amount is sent to the processing tank 10 through the path of the valve 7, the filter 8 or the valve 9.
.処理ドライ11をゆっくり回し、高沸点溶剤4aを処理
槽10、ボタントラップ12、バルブ13、ポンプ6、バルブ
7、フィルタ8、又はバルブ9から成る回路で循環して
衣料2を洗浄する。. The processing dry 11 is slowly rotated, and the high-boiling solvent 4a is circulated in the circuit including the processing tank 10, the button trap 12, the valve 13, the pump 6, the valve 7, the filter 8, and the valve 9 to wash the clothing 2.
.処理槽10、ボタントラップ12、バルブ13、ポンプ
6、バルブ14、蒸留器15の経路で排液し、つづいて処理
ドラム11が高速回転して衣料2中の高沸点溶剤4aを遠心
分離し、同様に排液する。. The liquid is discharged through the processing tank 10, the button trap 12, the valve 13, the pump 6, the valve 14, and the distiller 15. Then, the processing drum 11 rotates at a high speed to centrifuge the high-boiling solvent 4a in the clothing 2, Drain similarly.
.タンク3から低沸点溶剤4をバルブ5を介してポン
プ6により汲み揚げ、バルブ7、フィルタ8、又はバル
ブ9の経路で処理槽10に必要量を送り込む。. A low-boiling solvent 4 is pumped from a tank 3 by a pump 6 via a valve 5, and a required amount is sent to a processing tank 10 via a valve 7, a filter 8 or a valve 9.
.前記項と同じ(但し、高沸点溶剤4aを低沸点溶剤
4に読みかえる)。. Same as above (however, high-boiling solvent 4a is read as low-boiling solvent 4).
.前記項と同じ(但し、高沸点溶剤4aを低沸点溶剤
4に読みかえる)。. Same as above (however, high-boiling solvent 4a is read as low-boiling solvent 4).
.再び処理ドラム11をゆっくり回し、ファン16、エア
クーラ17、エアヒータ18から成るリカバリエアダクト19
と処理槽10の間を矢印20の向きでエアを循環させ、衣料
2を乾燥する。衣料2から蒸発した溶剤ガスはエアクー
ラ17で凝縮し、回収経路21を通って逆止弁31を経由して
蒸留器15に流入する。. The processing drum 11 is slowly rotated again, and a recovery air duct 19 including a fan 16, an air cooler 17, and an air heater 18 is provided.
The air is circulated in the direction of arrow 20 between and the processing tank 10 to dry the clothing 2. The solvent gas evaporated from the garment 2 is condensed in the air cooler 17 and flows into the distiller 15 through the recovery path 21 and the check valve 31.
.乾燥が終了すると、ダンパ25,26が破線の如く開
き、ダンパ25から新鮮な空気をとり入れてダンパ26から
のエアクーラ17では回収できない未凝縮溶剤ガスを排気
し、衣料2中の溶剤臭を脱臭する。. When the drying is completed, the dampers 25 and 26 open as indicated by broken lines, take in fresh air from the damper 25, exhaust the uncondensed solvent gas that cannot be recovered by the air cooler 17 from the damper 26, and deodorize the solvent odor in the clothing 2. .
.前記,,項の工程で蒸留器15に入った混合溶
剤(4+4a)は、先ず低沸点溶剤4で決まる融点で蒸留
され、コンデンサ27を経由し、蒸留温度センサ(図示せ
ず)でコントロールされ、開弁したバルブ32を介して水
分離器22に流入し、更に溶剤配管23を通ってタンク3に
戻る。. The mixed solvent (4 + 4a) that has entered the still 15 in the above steps is first distilled at the melting point determined by the low-boiling solvent 4, passed through the condenser 27, and controlled by a distillation temperature sensor (not shown). The water flows into the water separator 22 through the valve 32 that has been opened, and returns to the tank 3 through the solvent pipe 23.
次に蒸留器15中の低沸点溶剤が減少してくると、徐々
に沸点が高沸点溶剤4aの沸点に近づき、高沸点溶剤4aの
蒸留が開始されるようになるが、前記と同様蒸留温度セ
ンサ(図示せず)が作動して、バルブ32aを開弁(32は
閉弁)し、前記と同様にタンク3aに高沸点溶剤4aが回収
される(低沸点溶剤より高沸点溶剤への切替り時の中間
成分溶剤は、実験上微少量であって実用上問題とならな
いので、何れかの溶剤として取扱う)。Next, when the low-boiling solvent in the distiller 15 decreases, the boiling point gradually approaches the boiling point of the high-boiling solvent 4a, and the distillation of the high-boiling solvent 4a is started. A sensor (not shown) is operated to open the valve 32a (32 is closed), and the high boiling solvent 4a is recovered in the tank 3a in the same manner as described above (switch from the low boiling solvent to the high boiling solvent) The intermediate solvent at the time of removal is treated as any solvent since it is very small in the experiment and does not pose a practical problem.)
次に以上説明したような洗浄の途中、又は乾燥の直前
で高沸点溶剤を低沸点溶剤に置き換えることによる効果
の1例を第5図を用いて説明する。Next, an example of the effect of replacing the high-boiling solvent with the low-boiling solvent immediately before or during the washing as described above will be described with reference to FIG.
第5図は高津点溶剤としてパークロルエチレン、低沸
点溶剤としてR113を選び、ウールニット等の衣料10kgを
パークロルエチレンで洗浄、乾燥直前にフロンR113と置
き換え、即ちパークロルエチレンを脱液したのち、約25
のフロンR113で洗浄、脱液して、乾燥温度70〜80℃で
乾燥したときに得られたエアクーラ17での溶剤凝縮回収
曲線を、通常のパークロルエチレンによるウールニット
等の衣料10kgの洗浄、乾燥時のそれと比較したものであ
る。第5図から明らかなように、第4図による場合は従
来法に比べ、乾燥時間を半減することができる。なお、
ここではターペンとフロンR113等の他の組合せについて
の詳しい説明は省略するが、パークロルエチレンのケー
スと同様の効果が得られることは勿論である。Fig. 5 shows that perchlore ethylene is selected as the Takatsu point solvent and R113 is selected as the low boiling point solvent. 10 kg of clothing such as wool knit is washed with perchlorethylene and replaced with Freon R113 immediately before drying, that is, after the perchlorethylene is drained. , About 25
Washing and draining with CFC R113, solvent condensation and recovery curve in the air cooler 17 obtained when drying at a drying temperature of 70 to 80 ° C., washing of 10 kg of clothing such as wool knit with ordinary perchlor ethylene, It is a comparison with that at the time of drying. As is clear from FIG. 5, the drying time can be reduced by half in the case of FIG. 4 as compared with the conventional method. In addition,
Although the detailed description of other combinations such as tarpen and Freon R113 is omitted here, it goes without saying that the same effect as that of the case of perchlorethylene can be obtained.
(発明が解決しようとする課題) 以上の如く従来装置における溶剤の置き換えは優れた
特徴を有するが、同一機で2種類の溶剤を使用するた
め、作業者の勘違いによる操作ミス等により、溶剤が混
合して溶剤タンクに入ってしまうことが皆無とは云えな
い。従って実用上は、日常管理として定期的に溶剤タン
クの溶剤を抜出し、溶剤の比重を測定して確認している
のが実情である。しかしターペン以外は比重が近似して
いるため測定が困難で、判定に多くの時間と、人手を要
するなどの問題があると共に、溶剤を取り出すのは衛生
上好ましくなかった。(Problems to be Solved by the Invention) As described above, the replacement of the solvent in the conventional apparatus has an excellent feature. However, since two kinds of solvents are used in the same machine, the solvent may be lost due to an operation mistake due to an operator's misunderstanding. It cannot be said that there is absolutely no possibility of mixing and entering the solvent tank. Therefore, in practice, it is a fact that the solvent is periodically extracted from the solvent tank as a daily management and the specific gravity of the solvent is measured and confirmed. However, other than the terpene, the specific gravity is close to each other, so that the measurement is difficult, there is a problem that a lot of time and labor are required for the determination, and it is not preferable from the viewpoint of hygiene to remove the solvent.
また従来は、夫々の溶剤タンク内の溶剤の濃度を迅速
に測定して現在値を表示すると同時に、許容濃度範囲を
越えた場合は警報を発する等の動作を、高速、高信頼度
で行なう手段はなく、更に混合後の溶剤濃度が目的の濃
度範囲であることを確認して洗浄を開始する装置は従来
出現していなかった。Conventionally, means for quickly measuring the concentration of the solvent in each solvent tank and displaying the current value, and simultaneously issuing an alarm when the concentration exceeds the allowable concentration range, with high speed and high reliability. There has been no device that confirms that the solvent concentration after mixing is within a desired concentration range and starts cleaning.
本発明は前記の課題を解決するために提案されたもの
である。The present invention has been proposed to solve the above problems.
(課題を解決するための手段) このため本発明は、高沸点溶剤(4a)を貯留する溶剤
貯留タンク(3a)と、低沸点溶剤(4)を貯留する溶剤
貯留タンク(3)と、回転ドラム式の処理槽(10)と、
溶剤蒸留器(15)と、処理槽(10)へ前記の溶剤を選択
的に供給する溶剤供給手段を備え、ドライクリーニング
機械の制御装置(910)により、指定した機械の運転順
序(シーケンス)に基づき、処理槽(10)へ溶剤を選択
的に供給して衣料(2)を洗浄から脱液、乾燥まで処理
可能にしたドライクリーニング機械において、超音波セ
ンサ(110)と超音波発振受信手段(120)から成る超音
波測定手段(100)と、超音波の伝播時間計測手段(20
0)と、温度検出手段(300)と、音速演算回路(44
0),音波発振受信手段(120)及び超音波の伝播時間計
測手段(200)を制御する制御回路(410)と、超音波の
伝播速度と濃度の関係を示す音速特性記憶手段(430)
と、音速と測定部の温度と音速特性に基づき濃度を演算
する濃度演算手段(450)とを備え、測定場所の数に応
じて複数組に対配置した超音波センサ(110)及び温度
検出手段(300)と、各超音波センサ(110)と超音波発
振受信手段(120)を選択的に接続する超音波センサ選
択手段(601)及び温度検出手段(300)と濃度演算手段
(450)を選択的に接続する温度検出手段選択手段(60
2)から成るセンサ選択手段(600)と、目標値設定手段
(460)を設け、制御回路(410)の選択指令に応じて、
複数の指定場所に対応する混合液体の濃度を測定可能に
したマルチチャンネル型混合液体の濃度測定装置の各セ
ンサ対を、高沸点溶剤(4a)を貯留する溶剤貯留タンク
(3a)、低沸点溶剤(4)を貯留する溶剤貯留タン
(3)、処理槽(10)の底部に設けると共に、制御回路
(410)と制御装置(910)の入出力を連動させて、機械
の運転中の指定場所の溶剤の濃度を測定可能にしてなる
もので、これを課題解決のための手段とするものであ
る。(Means for Solving the Problems) For this reason, the present invention provides a solvent storage tank (3a) for storing a high-boiling solvent (4a), a solvent storage tank (3) for storing a low-boiling solvent (4), A drum-type treatment tank (10),
A solvent distillation unit (15) and a solvent supply means for selectively supplying the solvent to the treatment tank (10) are provided. The dry cleaning machine controller (910) controls the designated machine operation sequence (sequence). Based on the ultrasonic sensor (110) and the ultrasonic oscillation receiving means (1), in a dry cleaning machine in which a solvent can be selectively supplied to the processing tank (10) and the clothing (2) can be processed from washing to dewatering and drying. 120) and an ultrasonic propagation time measuring means (20).
0), the temperature detection means (300), and the sound velocity calculation circuit (44
0), a control circuit (410) for controlling the sound wave oscillation receiving means (120) and the ultrasonic wave propagation time measuring means (200), and a sound velocity characteristic storage means (430) indicating the relationship between the ultrasonic wave propagation velocity and the concentration
And an ultrasonic sensor (110) and a temperature detecting means arranged in a plurality of pairs according to the number of measurement places, comprising: a density calculating means (450) for calculating a density based on a sound speed, a temperature of the measuring section and a sound speed characteristic. (300), ultrasonic sensor selecting means (601) for selectively connecting each ultrasonic sensor (110) and ultrasonic oscillation receiving means (120), temperature detecting means (300), and concentration calculating means (450). Temperature detection means selection means (60
2) a sensor selection means (600) composed of 2) and a target value setting means (460) are provided, and according to a selection command of the control circuit (410),
Each sensor pair of the multi-channel type mixed liquid concentration measurement device that can measure the concentration of the mixed liquid corresponding to a plurality of designated locations is connected to a solvent storage tank (3a) for storing a high boiling solvent (4a) and a low boiling solvent The solvent storage tank (3) for storing (4) is provided at the bottom of the processing tank (10), and the input / output of the control circuit (410) and the control device (910) are linked to specify a designated place during operation of the machine. This makes it possible to measure the concentration of the solvent, and this is used as a means for solving the problem.
(作用) 相溶性ある二成分混合液体内を伝播する音圧の伝播速
度は、例えばパークロルエチレンとフロン113の測定例
から V=V(t・P)で表わされる。(Operation) The propagation speed of the sound pressure propagating in the compatible two-component mixed liquid is represented by V = V (t · P) from a measurement example of perchlorethylene and Freon 113, for example.
但し V:音速 m/s t:温度 ℃ P:濃度 vol% or wt% 従ってtとVを求めれば、Pは演算によって求められ
る。また超音波測定手段と伝播時間計測手段により定距
離Lを伝播する音波伝播時間τを求めて、演算制御装置
によりV=L/τを求め、これと温度測定結果とV=V
(t・P)の関係からP及び1−Pを演算によって求め
る。結果は表示手段に示す。更に複数の超音波センサと
温度検出手段を選択切換えて、マルチチャンネル型濃度
測定装置を得る。However, V: sound velocity m / st: temperature ℃ P: concentration vol% or wt% Therefore, if t and V are obtained, P can be obtained by calculation. Also, the ultrasonic wave propagation means and the propagation time measurement means determine the sound wave propagation time τ propagating through the fixed distance L, and the arithmetic and control unit calculates V = L / τ.
P and 1−P are obtained by calculation from the relationship of (t · P). The results are shown on the display. Further, a plurality of ultrasonic sensors and temperature detecting means are selectively switched to obtain a multi-channel type concentration measuring device.
(実施例) 以下本発明を図面の実施例について説明すると、第1
図は第1実施例であるマルチチャンネル型濃度測定警報
装置を示し、第2図は第2実施例であるマルチチャンネ
ル型濃度測定警報装置を装備したドライクリーニング機
械を示す。(Embodiments) The present invention will be described below with reference to the embodiments in the drawings.
FIG. 1 shows a multi-channel type concentration measuring and alarming device according to a first embodiment, and FIG. 2 shows a dry cleaning machine equipped with a multi-channel type concentration measuring and alarming device according to a second embodiment.
先ず第1図において、100は超音波測定手段、110は超
音波センサ、111は送波子、112は受波子、120は超音波
発振受信手段、121は高周波パルス発生手段、122は電圧
増幅手段、200は伝播時間計測手段、210は受信パルス発
生手段、211は増幅比較手段、212はパルス回路、220は
時間計数手段、221はクロック回路、222は種算回路、30
0は温度検出手段、400は演算制御装置、410は制御回
路、420は開始信号発生手段、430は音速特性記憶手段、
440は音速演算回路、450は濃度演算手段、500は表示手
段である。First, in FIG. 1, 100 is an ultrasonic measuring means, 110 is an ultrasonic sensor, 111 is a transmitter, 112 is a receiver, 120 is an ultrasonic oscillation receiving means, 121 is a high-frequency pulse generating means, 122 is a voltage amplifying means, 200 is a propagation time measuring means, 210 is a received pulse generating means, 211 is an amplification comparing means, 212 is a pulse circuit, 220 is a time counting means, 221 is a clock circuit, 222 is a seed circuit, 30
0 is a temperature detecting means, 400 is an arithmetic and control unit, 410 is a control circuit, 420 is a start signal generating means, 430 is a sound speed characteristic storing means,
Reference numeral 440 is a sound speed calculation circuit, 450 is a density calculation means, and 500 is a display means.
さて超音波センサ110は、温度検出手段300と対にして
濃度を測定すべき液体中に設置されており、かつ送波子
111は圧電体等で構成され、超音波発振受信手段120の高
周波パルス発生手段121により、圧電体の固有振動数と
同じ周波数成分を多く持つ単発性のパルス電圧が印加さ
れると、圧電体には微小な変位が生じ、これを駆動源と
して送波子111と接する液面に歪が誘起され、波動とし
て伝播する。また受波子112はやはり圧電体で構成さ
れ、音圧による歪により電圧を出力する。そしてこの電
圧は超音波発振受信手段120の電圧増幅手段122に入力さ
れ、増幅された電圧Viが出力される。Now, the ultrasonic sensor 110 is installed in the liquid whose concentration is to be measured in pairs with the temperature detecting means 300, and
111 is composed of a piezoelectric body or the like, and when a single pulse voltage having many of the same frequency components as the natural frequency of the piezoelectric body is applied by the high-frequency pulse generating means 121 of the ultrasonic oscillation receiving means 120, Causes a small displacement, which is used as a drive source to induce a strain on the liquid surface in contact with the transmitter 111 and propagate as a wave. The receiver 112 is also formed of a piezoelectric material, and outputs a voltage due to distortion due to sound pressure. This voltage is input to the voltage amplifying unit 122 of the ultrasonic oscillation receiving unit 120, and the amplified voltage Vi is output.
次に伝播時間計測手段200について説明すると、これ
は受信パルス発生手段210と時間計数手段220によって構
成される。受信パルス発生手段210は電圧増幅手段122の
出力電圧を要すれば増幅し、比較手段211に予め設定さ
れた閾値Vsと比較することにより、Vi>Vs(Viの増幅率
βならβVi>Vs)ならパルス回路212に電圧を出力し、
パルス回路212によってパルスが出力される。Next, the propagation time measuring means 200 will be described. The transmitting time measuring means 200 is constituted by a reception pulse generating means 210 and a time counting means 220. The receiving pulse generating means 210 amplifies the output voltage of the voltage amplifying means 122 if necessary, and compares it with a threshold value Vs preset in the comparing means 211 to obtain Vi> Vs (βVi> Vs if the gain of Vi is β). If so, output a voltage to the pulse circuit 212,
A pulse is output by the pulse circuit 212.
時間計数手段220はクロック回路221及び積算回路222
によって構成される。また演算制御装置400の開始信号
発生手段の出力を時間起点とし、高周波パルス発生手段
121のパルス発信と、クロック回路221のクロックパルス
を積算回路222が積算開始し、受信パルス発生手段210の
パルス出力と同時に積算を停止し積算数Nを出力する。The time counting means 220 includes a clock circuit 221 and an integrating circuit 222.
Composed of The output of the start signal generating means of the arithmetic and control unit 400 is used as a time starting point, and the high-frequency pulse generating means is used.
The integration of the pulse transmission of 121 and the integration of the clock pulse of the clock circuit 221 is started by the integration circuit 222, and the integration is stopped simultaneously with the output of the pulse from the reception pulse generation means 210, and the integration number N is output.
更に演算制御装置400は、装置全体の制御を司る制御
回路410、同制御回路410の指令を受けて開始信号を出力
する開始手段420、音速特性V=V(t・P)を記憶す
る音速特性記憶手段430、伝播時間計測手段200の出力よ
り音速Vを はクロック回路221のクロック周波数)で演算する音速
演算回路440と温度検出手段300の検出温度tと、音速特
性記憶手段430の音速特性V=V(t・P)より濃度P
をP=V-1(t・P)なる逆演算で求める濃度演算手段4
50より構成され、濃度演算結果は表示手段500に測定液
体の種類と共に出力する。また表示手段500は前記出力
を表示する。このようにして制御回路410を外部トリガ
Rが入力すれば、前述の手順により濃度が測定表示され
る。この測定は制御回路の構成により複数回の測定結果
を平均値として表示することも容易に行える。Further, the arithmetic and control unit 400 includes a control circuit 410 for controlling the entire apparatus, a start means 420 for outputting a start signal in response to a command from the control circuit 410, and a sonic characteristic for storing a sonic characteristic V = V (t · P). The sound velocity V is obtained from the output of the storage means 430 and the propagation time measuring means 200. Is the density P from the detected temperature t of the sound speed calculating circuit 440 and the temperature detecting means 300 calculated by the clock frequency of the clock circuit 221 and the sound speed characteristic V = V (t · P) of the sound speed characteristic storing means 430.
Calculating means 4 for obtaining the following by the inverse operation of P = V -1 (tP)
The concentration calculation result is output to the display means 500 together with the type of the measurement liquid. The display means 500 displays the output. When the external trigger R is input to the control circuit 410 in this manner, the density is measured and displayed by the above-described procedure. This measurement can be easily performed by displaying the results of a plurality of measurements as an average value by the configuration of the control circuit.
また超音波センサを夫々のセンサ選択手段601,620よ
り成る選択手段600を設け、制御回路410により対応する
センサ対を択一的に選択するよう制御すれば、マルチチ
ャンネル型濃度測定装置を得る。第1図はマルチチャン
ネル型濃度測定警報装置を示す。図において600は選択
手段、601は超音波センサ選択手段、602は温度検出手段
選択手段、460は目標値設定手段、470は比較手段、700
は警報手段である。Further, when the ultrasonic sensor is provided with a selection means 600 comprising sensor selection means 601 and 620, and the control circuit 410 controls to selectively select a corresponding sensor pair, a multi-channel type concentration measuring device is obtained. FIG. 1 shows a multi-channel type concentration measurement alarm device. In the figure, 600 is a selecting means, 601 is an ultrasonic sensor selecting means, 602 is a temperature detecting means selecting means, 460 is a target value setting means, 470 is a comparing means, 700
Is an alarm means.
さて複数の超音波センサと温度検出手段を一対にして
選択する選択手段600と警報手段700を設け、演算制御装
置400に目標値設定手段460、比較手段470を増設し、制
御回路410を目標値設定手段460に目標値を設定する機能
と、選択手段600を制御する機能を追加し、比較手段470
は農度演算手段450の出力と前記目標値を比較して異常
の有無を判断し、異常なら警報手段700に異常信号を出
力するよう構成されている。Now, a selecting means 600 and a warning means 700 for selecting a plurality of ultrasonic sensors and temperature detecting means as a pair are provided, a target value setting means 460 and a comparing means 470 are added to the arithmetic and control unit 400, and the control circuit 410 sets the target value to the target value. A function for setting a target value and a function for controlling the selecting means 600 are added to the setting means 460, and the comparing means 470 is added.
Is configured to compare the output of the agricultural degree calculation means 450 with the target value to determine the presence or absence of an abnormality, and to output an abnormality signal to the alarm means 700 if abnormal.
また外部からトリガ信号Rが入力されると、制御回路
410は所定の超音波センサと温度検出手段を選択手段600
によって選択すると同時に、目標値設定手段460に目標
値を設定し、濃度測定を開始する。また濃度演算手段45
0の出力は比較手段470により目標値と比較され、異常の
有無を判別して、異常の時は警報手段700に異常信号を
出力する。When a trigger signal R is input from the outside, the control circuit
410 is a predetermined ultrasonic sensor and temperature detecting means selecting means 600
At the same time, the target value is set in the target value setting means 460, and the concentration measurement is started. In addition, density calculation means 45
The output of 0 is compared with the target value by the comparing means 470 to determine the presence or absence of an abnormality.
第2図は第1図に示すマルチチャンネル型濃度測定警
報装置を設置したドライクリーニング機械を示す。図に
おいて符号1〜33のドライクリーニング機械における各
部分は第4図と同一であるので、これらの詳細な説明は
省略し、第5図との相違点を説明すると、900はドライ
クリーニング機械、910はドライクリーニング機械の制
御装置、920は処理槽10に設けた溶剤溜、930は溶剤回収
配管、800はマルチチャンネル型濃度測定警報装置、300
C,300A,300Bは超音波センサ、100C,100A,100Bは温度検
出手段である。FIG. 2 shows a dry cleaning machine provided with the multi-channel type concentration measuring and alarming device shown in FIG. In the figure, the respective parts in the dry cleaning machine denoted by reference numerals 1 to 33 are the same as those in FIG. 4, and therefore detailed description thereof will be omitted, and the differences from FIG. 5 will be described. Is a control device of a dry cleaning machine, 920 is a solvent reservoir provided in the processing tank 10, 930 is a solvent recovery pipe, 800 is a multi-channel type concentration measurement alarm device, 300
C, 300A and 300B are ultrasonic sensors, and 100C, 100A and 100B are temperature detecting means.
さてマルチチャンネル濃度測定警報装置800は、制御
回路410の外部トリガ信号と、警報手段700の出力がドラ
イクリーニング機械の制御装置910と協調して接続され
る他は、第2図に示したものと基本的に同一である。Now, the multi-channel concentration measurement alarm device 800 is the same as that shown in FIG. 2 except that the external trigger signal of the control circuit 410 and the output of the alarm means 700 are connected in cooperation with the control device 910 of the dry cleaning machine. Basically the same.
またドライクリーニング機械900は、処理槽10の底部
に溶剤溜920と溶剤排出管930を設けると共に、溶剤タン
ク3a,3、溶剤溜920に夫々超音波センサと温度センサを
対にして100A,300A,100C,300C,100B,300Bを設けた他
は、第4図の従来例と同一である。一方濃度測定警報装
置の演算制御手段400の制御回路410は、ドライクリーニ
ング機械900の制御装置910の指令を外部トリガ入力とし
て測定を開始し、警報手段700の出力を介して、異常が
あれば制御装置910に指令を送って機械停止等の処理を
行うことができる。またドライクリーニングの洗浄工程
の進行に合せて、所望のタンク内の濃度を知ることもで
きる。更に音速特性記憶手段430には複数種の二成分混
合液体の音速特性を、目標値設定手段460には対応する
目標値を設定して、制御回路410でドライクリーニング
機械の使用溶剤の種類に応じて選択することを実現する
ことは、現今のデータ処理技術水準では容易であるから
可能である。In addition, the dry cleaning machine 900 is provided with a solvent reservoir 920 and a solvent discharge pipe 930 at the bottom of the processing tank 10, and a pair of ultrasonic sensors and temperature sensors in the solvent tanks 3a and 3 and the solvent reservoir 920, respectively. Except that 100C, 300C, 100B, and 300B are provided, it is the same as the conventional example of FIG. On the other hand, the control circuit 410 of the arithmetic and control means 400 of the concentration measurement and alarm device starts the measurement by using the command of the control device 910 of the dry cleaning machine 900 as an external trigger input, and controls the output of the alarm means 700 to control if there is any abnormality. A command can be sent to the device 910 to perform processing such as stopping the machine. In addition, the desired concentration in the tank can be known as the cleaning process of the dry cleaning proceeds. Further, the sonic velocity characteristic storage means 430 sets the sonic velocity characteristics of a plurality of types of two-component mixed liquids, and the target value setting means 460 sets corresponding target values, and the control circuit 410 controls the type of solvent used in the dry cleaning machine. It is possible to realize the selection by using the current data processing technology.
ここで二成分混合液体濃度測定装置の構成手段につい
て説明する。Here, the constituent means of the two-component mixed liquid concentration measuring device will be described.
(1) 相溶性ある二成分混合液体内を伝播する音圧の
伝播速度は、例えば第3図に示すパークロルエチレンと
フロン113の測定例の様に、 V=V(t・P)で表わされる。(1) The propagation speed of sound pressure propagating in a compatible binary liquid mixture is expressed by V = V (t · P), for example, as shown in the measurement example of perchlor ethylene and fluorocarbon 113 shown in FIG. It is.
但し V:音速 m/s t:温度 ℃ P:濃度 vol% or wt% 従ってtとVを求めれば、Pは演算によって求められ
る。However, V: sound velocity m / st: temperature ℃ P: concentration vol% or wt% Therefore, if t and V are obtained, P can be obtained by calculation.
(2) 超音波測定手段100と伝播時間計測手段200によ
り定距離Lを伝播する音波伝播時間τを求めて、演算制
御装置400によりV=L/τを求め、これと温度測定結果
とV=V(t・P)の関係からP及び1−Pを演算によ
って求める。結果は表示手段500に示す。(2) The ultrasonic wave propagation means 100 and the propagation time measurement means 200 determine the sound wave propagation time τ propagating through the fixed distance L, and the arithmetic and control unit 400 calculates V = L / τ. P and 1−P are obtained by calculation from the relationship of V (t · P). The result is shown on display means 500.
(3) 複数の超音波センサ110と温度検出手段300を選
択切換えて、マルチチャンネル型濃度測定装置を得る。(3) A plurality of ultrasonic sensors 110 and temperature detecting means 300 are selectively switched to obtain a multi-channel type concentration measuring device.
(発明の効果) 以上詳細に説明した如く本発明は構成されているの
で、音速センサと温度センサを対にして複数個設置する
だけで、複数個所の異なった溶剤に対する濃度を計測で
きると共に、安価に提供できる。また計測時間が短くな
るので、ドライクリーニング機械に適用した場合、その
サイクルタイムを長くする不具合がない。更にドライク
リーニング機械の場合、溶剤濃度不良に基因する衣料事
故を防止できる。(Effects of the Invention) As described in detail above, the present invention is configured, so that by simply installing a plurality of sound speed sensors and temperature sensors in pairs, it is possible to measure the concentration of the solvent at a plurality of different locations and to reduce the cost. Can be provided. Further, since the measurement time is shortened, there is no problem that the cycle time is lengthened when applied to a dry cleaning machine. Further, in the case of a dry cleaning machine, clothing accidents due to poor solvent concentration can be prevented.
本発明は検出端を複数配置して、検出端を選択的に切
り替え動作させ、指定位置の濃度を選択的に検出可能に
する点に特徴があり、また沸点の異なる2種の溶剤を用
いるドライクリーニング機械において、各溶剤の貯留槽
及び夫々の溶剤が交互に入替え注入される処理槽に、濃
度測定装置を設けることにより、検出端を選択切替える
のみで、機械の運転サイクルに対応して状態が変化する
処理槽の溶剤濃度、及び蒸留器の分流精度の影響を受け
て変化する恐れのある各溶剤貯留槽の濃度の異常の有無
の管理を容易に行うことができる。The present invention is characterized in that a plurality of detection ends are arranged, the detection ends are selectively switched, and the concentration at a designated position can be selectively detected. In a cleaning machine, by installing a concentration measuring device in the storage tank of each solvent and the processing tank in which each solvent is alternately injected, only the detection end is selectively switched, and the state corresponding to the machine operation cycle is changed. It is possible to easily manage whether or not there is an abnormality in the concentration of each of the solvent storage tanks, which may change due to the changing solvent concentration in the treatment tank and the branching accuracy of the still.
得に超音波の伝播時間計測手段、超音波発振受信手
段、演算制御手段の主要部を共通にしながら、目的とす
る所要場所の濃度を機械の運転中にも選択的に管理し、
要すれば警報することを容易に実施できるドライクリー
ニング機械を提供できる。In particular, while ultrasonic transmission time measuring means, ultrasonic oscillation receiving means, the main part of the arithmetic control means in common, selectively manage the concentration of the desired required location during the operation of the machine,
If necessary, it is possible to provide a dry cleaning machine that can easily perform an alarm.
第1図は本発明の実施例を示すマルチチャンネル型濃度
測定警報装置のブロック図、第2図は同ドライクリーニ
ング機械に適用した場合のブロック図、第3図は音速特
性の測定例を示す特性線図、第4図は従来のドライクリ
ーニング機械の回路図、第5図は従来の2種溶剤を使用
する効果の例を示す線図である。 図の主要部分の説明 100……超音波測定手段、111……送波子 112……受波子、111′……送受波子 112′……反射板 121……高周波パルス発生手段 122……電圧増幅手段 200……伝播時間計測手段 210……受信パルス発生手段 211……比較手段、212……パルス回路 220……時間計数手段、221……クロック回路 222……積算回路、300……温度検出手段 400……演算制御手段、410……制御回路 420……開始信号発生手段 430……音速特性記憶手段、440……音速演算回路 450……濃度演算手段、500……表示手段FIG. 1 is a block diagram of a multi-channel type concentration measuring and alarming device showing an embodiment of the present invention, FIG. 2 is a block diagram when applied to the dry cleaning machine, and FIG. 3 is a characteristic showing a measurement example of sound speed characteristics. FIG. 4 is a circuit diagram of a conventional dry cleaning machine, and FIG. 5 is a diagram illustrating an example of the effect of using two conventional solvents. Description of main parts in the drawing 100 ultrasonic measuring means 111 transmitting element 112 receiving element 111 'transmitting and receiving element 112' reflecting plate 121 high frequency pulse generating means 122 voltage amplifying means 200 propagation time measuring means 210 received pulse generating means 211 comparing means 212 pulse circuit 220 time counting means 221 clock circuit 222 integrating circuit 300 temperature detecting means 400 Calculation control means 410 Control circuit 420 Start signal generation means 430 Sound velocity characteristic storage means 440 Sound velocity calculation circuit 450 Density calculation means 500 Display means
───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 敏夫 愛知県名古屋市中村区岩▲塚▼町字高道 1番地 三菱重工業株式会社名古屋研究 所内 (56)参考文献 特開 平2−203899(JP,A) 実開 昭63−111890(JP,U) ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Toshio Hattori No. 1, Iwa-tsuka ▼ -machi, Takamichi, Nakamura-ku, Nagoya-shi, Aichi Nagoya Laboratory, Mitsubishi Heavy Industries, Ltd. (56) References JP-A-2-203899 (JP) , A) Actually open 1988-111890 (JP, U)
Claims (1)
ク(3a)と、低沸点溶剤(4)を貯留する溶剤貯留タン
ク(3)と、回転ドラム式の処理槽(10)と、溶剤蒸留
器(15)と、処理槽(10)へ前記の溶剤を選択的に供給
する溶剤供給手段を備え、ドライクリーニング機械の制
御装置(910)により、指定した機械の運転順序(シー
ケンス)に基づき、処理槽(10)へ溶剤を選択的に供給
して衣料(2)を洗浄から脱液、乾燥まで処理可能にし
たドライクリーニング機械において、超音波センサ(11
0)と超音波発振受信手段(120)から成る超音波測定手
段(100)と、超音波の伝播時間計測手段(200)と、温
度検出手段(300)と、音速演算回路(440),音波発振
受信手段(120)及び超音波の伝播時間計測手段(200)
を制御する制御回路(410)と、超音波の伝播速度と濃
度の関係を示す音速特性記憶手段(430)、音速と測定
部の温度と音速特性に基づき濃度を演算する濃度演算手
段(450)とを備え、測定場所の数に応じて複数組に対
配置した超音波センサ(110)及び温度検出手段(300)
と、各超音波センサ(110)と超音波発振受信手段(12
0)を選択的に接続する超音波センサ選択手段(601)及
び温度検出手段(300)と濃度演算手段(450)を選択的
に接続する温度検出手段選択手段(602)から成るセン
サ選択手段(600)と、目標値設定手段(460)を設け、
制御回路(410)の選択指令に応じて、複数の指定場所
に対応する混合液体の濃度を測定可能にしたマルチチャ
ンネル型混合液体の濃度測定装置の各センサ対を、高沸
点溶剤(4a)を貯留する溶剤貯留タンク(3a)、低沸点
溶剤(4)を貯留する溶剤貯留タン(3)、処理槽(1
0)の底部に設けると共に、制御回路(410)と制御装置
(910)の入出力を連動させて、機械の運転中の指定場
所の溶剤の濃度を測定可能にしたドライクリーニング機
械。A solvent storage tank (3a) for storing a high-boiling solvent (4a), a solvent storage tank (3) for storing a low-boiling solvent (4), a rotary drum type processing tank (10), A solvent distillation unit (15) and a solvent supply means for selectively supplying the solvent to the treatment tank (10) are provided. The dry cleaning machine controller (910) controls the designated machine operation sequence (sequence). Based on the ultrasonic sensor (11), in a dry cleaning machine in which the solvent (2) can be processed from washing to dewatering and drying by selectively supplying a solvent to the processing tank (10).
0), an ultrasonic measuring means (100) comprising an ultrasonic oscillation receiving means (120), an ultrasonic wave propagation time measuring means (200), a temperature detecting means (300), a sound velocity calculation circuit (440), a sound wave Oscillation receiving means (120) and ultrasonic propagation time measuring means (200)
Control circuit (410), and a sound speed characteristic storage unit (430) indicating the relationship between the propagation speed of ultrasonic waves and the concentration, and a concentration calculation unit (450) for calculating the concentration based on the sound speed, the temperature of the measuring unit, and the sound speed characteristics And ultrasonic sensors (110) and temperature detecting means (300) arranged in pairs in accordance with the number of measurement locations.
And each ultrasonic sensor (110) and ultrasonic oscillation receiving means (12
(0) and a sensor selection means (602) comprising temperature detection means selection means (602) for selectively connecting temperature detection means (300) and concentration calculation means (450). 600) and target value setting means (460)
According to the selection command of the control circuit (410), each sensor pair of the multi-channel type mixed liquid concentration measuring device capable of measuring the concentration of the mixed liquid corresponding to a plurality of designated locations is connected to the high boiling solvent (4a). The solvent storage tank (3a) for storing the solvent, the solvent storage tank (3) for storing the low boiling point solvent (4), and the treatment tank (1
0) A dry cleaning machine which is provided at the bottom of the apparatus and which enables the measurement of the solvent concentration at a designated place during operation of the machine by linking the input / output of the control circuit (410) and the input / output of the control device (910).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1072833A JP2634232B2 (en) | 1989-03-24 | 1989-03-24 | Dry cleaning machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1072833A JP2634232B2 (en) | 1989-03-24 | 1989-03-24 | Dry cleaning machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02249964A JPH02249964A (en) | 1990-10-05 |
| JP2634232B2 true JP2634232B2 (en) | 1997-07-23 |
Family
ID=13500812
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1072833A Expired - Fee Related JP2634232B2 (en) | 1989-03-24 | 1989-03-24 | Dry cleaning machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2634232B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002071646A (en) * | 2000-08-28 | 2002-03-12 | Kyoto Electron Mfg Co Ltd | Liquid concentration measurement method |
| JP2019066410A (en) * | 2017-10-04 | 2019-04-25 | 株式会社ディスコ | Measuring instrument and processing device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3112002A1 (en) * | 1981-03-26 | 1982-10-14 | Siemens AG, 1000 Berlin und 8000 München | DEVICE FOR MONITORING THE CONCENTRATION OF AN AIR-VAPOR MIXTURE IN THE FIXING STATION OF A NON-MECHANICAL PRINT OR COPIER |
| JPS5877656A (en) * | 1981-11-04 | 1983-05-11 | Fuji Kogyo Kk | Ultrasonic measuring device for concentration |
| JPS6225254A (en) * | 1985-07-25 | 1987-02-03 | Toyota Motor Corp | Method and apparatus for detecting mixing ratio of mixed fuel |
-
1989
- 1989-03-24 JP JP1072833A patent/JP2634232B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02249964A (en) | 1990-10-05 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |