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JP2744665B2 - Solvent recovery equipment for dry cleaning equipment - Google Patents

Solvent recovery equipment for dry cleaning equipment

Info

Publication number
JP2744665B2
JP2744665B2 JP2016073A JP1607390A JP2744665B2 JP 2744665 B2 JP2744665 B2 JP 2744665B2 JP 2016073 A JP2016073 A JP 2016073A JP 1607390 A JP1607390 A JP 1607390A JP 2744665 B2 JP2744665 B2 JP 2744665B2
Authority
JP
Japan
Prior art keywords
air
solvent
processing tank
conduit
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 - Lifetime
Application number
JP2016073A
Other languages
Japanese (ja)
Other versions
JPH03221098A (en
Inventor
喜代美 山田
信治 高木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP2016073A priority Critical patent/JP2744665B2/en
Publication of JPH03221098A publication Critical patent/JPH03221098A/en
Application granted granted Critical
Publication of JP2744665B2 publication Critical patent/JP2744665B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はドライクリーナの乾燥、脱臭工程に適用され
るドライクリーニング装置の溶剤回収装置に関するもの
である。
Description: TECHNICAL FIELD The present invention relates to a solvent recovery device of a dry cleaning device applied to a drying and deodorizing step of a dry cleaner.

(従来の技術) 第3図に従来におけるドライクリーニング装置の溶剤
回収装置を示す。第3図において処理槽1内には衣類が
投入されて回転され、溶媒により処理される。そして洗
浄処理後の乾燥時には、乾燥空気は処理槽1を通過し、
この乾燥空気は送風機2により吸気管3及びリントフィ
ルタ4を介して吸込まれると共に、水冷却器5と冷媒冷
却器6に押込まれる。更にこの空気は切換弁10が第3図
のように閉じている場合は、加熱器7を通って加熱され
る。
(Prior Art) FIG. 3 shows a conventional solvent recovery device of a dry cleaning device. In FIG. 3, clothes are put into the treatment tank 1 and rotated, and treated with a solvent. Then, at the time of drying after the cleaning process, the dry air passes through the processing tank 1,
The dry air is sucked by the blower 2 through the intake pipe 3 and the lint filter 4 and pushed into the water cooler 5 and the refrigerant cooler 6. Further, this air is heated through the heater 7 when the switching valve 10 is closed as shown in FIG.

次いで衣類に付着する少量の溶剤分を、外気で蒸発さ
せるための脱臭工程が行われる。この場合は2点鎖線の
如く開いているダンパ11の開口部から外気を取り入れ、
処理槽1の中の衣類と接触させて脱臭し、リントフィル
タ4、送風機2、水冷却器5、冷媒冷却器6と経由し、
この溶剤ガスを含んだ空気は脱臭口20を経て機外に送ら
れる。この時切換弁10は2点鎖線の位置にある。なお、
この溶剤ガスを含んだ空気は、大気汚染防止の規制から
活性炭回収装置(図示しない)を経由して大気放出する
のが普通である。
Next, a deodorizing step for evaporating a small amount of solvent adhering to the clothes with outside air is performed. In this case, outside air is taken in from the opening of the damper 11 which is open as indicated by a two-dot chain line,
The deodorant is brought into contact with the clothes in the processing tank 1 and deodorized, and passes through a lint filter 4, a blower 2, a water cooler 5, and a refrigerant cooler 6,
The air containing the solvent gas is sent out of the machine through the deodorizing port 20. At this time, the switching valve 10 is at the position indicated by the two-dot chain line. In addition,
Normally, the air containing the solvent gas is released to the atmosphere via an activated carbon recovery device (not shown) due to regulations on air pollution prevention.

(発明が解決しようとする課題) 第3図の従来装置においては、処理槽内において衣類
より溶剤が蒸発した後、溶剤ガスは空気の2〜3倍の重
さがあるので処理槽の下部に溜り勝ちであるが、処理槽
より空気を吸出すための吸気管3に繋がる空気吸出し口
は処理槽の上方にあるので、空気の流れが処理槽上部に
偏り、乾燥時も脱臭時も溶剤ガスを吸出すための効率が
悪く、従って処理に時間がかかり、時には溶剤ガスが衣
類に付着したまま取り出される虞れがあった。
(Problem to be Solved by the Invention) In the conventional apparatus shown in FIG. 3, after the solvent evaporates from the clothes in the processing tank, the solvent gas weighs two to three times as much as air, so Although the air tends to accumulate, the air suction port connected to the suction pipe 3 for sucking air from the processing tank is located above the processing tank. The efficiency of sucking out the gas is low, so that it takes a long time for the treatment, and there is a possibility that the solvent gas is sometimes taken out while adhering to the clothes.

本発明は前記従来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-mentioned conventional problems.

(課題を解決するための手段) このため本発明は、処理槽からリントフィルタ、送風
機、冷却器及び加熱器を経て同処理槽に帰還する循環路
を有するドライクリーニング装置において、同処理槽下
部から処理槽上部の空気吹出し用導管にバイパス導管を
設けると共に、同空気吹出し用導管に絞り弁を設け、乾
燥工程では同絞り弁を開けて充分に空気を通し、脱臭工
程では同絞り弁を閉じることにより、空気は溶剤用の導
管と前記バイパス導管を通って前記リントフィルタ及び
送風機へと流れるようにしてなるもので、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 dry cleaning apparatus having a circulation path that returns from a processing tank to the processing tank via a lint filter, a blower, a cooler, and a heater. Provide a bypass conduit in the air outlet conduit at the top of the treatment tank, and provide a throttle valve in the air outlet conduit.Open the throttle valve in the drying process to allow sufficient air to flow, and close the throttle valve in the deodorization process. This allows air to flow through the solvent conduit and the bypass conduit to the lint filter and the blower, which is a means for solving the problem.

(作用) 溶剤ガスが処理槽の下部に残り勝ちのことに着眼し、
処理槽の下部から処理槽上部の空気吸出し用導管にバイ
パス管を設けると共に、同導管に絞り弁を設け、乾燥時
には処理槽の上部と下部からガス混りの空気を吸出して
空気用冷却器で液化し、空気を加熱して処理槽へと循環
させることにより、溶剤ガスの大部分を液化回収する。
また次の脱臭工程では、新しい空気を処理槽に入れなが
ら希薄なガスを含んだ空気を処理槽の下部の吸出し口か
らのみ空気冷却器へ送り、更に活性炭吸着器へ送って溶
剤の回収率を上げる。
(Action) Focusing on the fact that the solvent gas remains at the bottom of the processing tank,
A bypass pipe is provided from the lower part of the processing tank to the air suction pipe at the upper part of the processing tank, and a throttle valve is provided in the same pipe.At the time of drying, gas-mixed air is sucked from the upper part and the lower part of the processing tank and the air cooler is used. Most of the solvent gas is liquefied and recovered by liquefaction and heating and circulating the air to the treatment tank.
In the next deodorization step, while containing fresh air, the air containing the dilute gas is sent to the air cooler only from the suction port at the bottom of the processing tank, and then sent to the activated carbon adsorber to increase the solvent recovery rate. increase.

(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
図及び第2図は本発明の実施例を示すもので、両図とも
ドライクリーナの処理槽と溶剤ガスと空気が流れる風路
を示すもので、第1図は乾燥工程、第2図は脱臭工程の
空気の流れ状況を示す。
(Embodiments) The present invention will be described below with reference to the embodiments in the drawings.
FIGS. 2 and 3 show an embodiment of the present invention. Both figures show a treatment tank of a dry cleaner and an air passage through which solvent gas and air flow. FIG. 1 shows a drying process, and FIG. The flow of air in the process is shown.

先ず第1図において1は処理槽で、この中に外周が多
孔板になっている回転するドラムが設けられており、同
ドラムの中に衣類などの洗濯物を入れる。また2は空気
及び溶剤ガスを処理槽1及び風路を循環させる送風機で
ある。3は処理槽1より空気と溶剤ガスを吸出す吸気管
(空気吸出し用導管)で、風路の一部を形成している。
4は洗濯物から遊離する糸屑を取り除くリントフィル
タ、5は水冷却器、6は冷媒冷却器、7は加熱器、8は
処理槽1の入口側の風路を形成する導管、9は吸気管3
に設けられた絞り弁、10は切換弁で、この弁10の切換え
により空気の流れは循環から排出口20よりの排出に変え
られる。
First, in FIG. 1, reference numeral 1 denotes a processing tank, in which a rotating drum having a perforated outer periphery is provided, and laundry such as clothes is put in the drum. Reference numeral 2 denotes a blower for circulating air and a solvent gas through the processing tank 1 and the air passage. Reference numeral 3 denotes an air suction pipe (air suction pipe) for sucking air and solvent gas from the processing tank 1 and forms a part of an air passage.
4 is a lint filter for removing lint released from the laundry, 5 is a water cooler, 6 is a refrigerant cooler, 7 is a heater, 8 is a conduit forming an air passage on the inlet side of the processing tank 1, and 9 is intake air. Tube 3
Is a switching valve, and the switching of the valve 10 changes the flow of air from circulation to discharge from the discharge port 20.

11は外気取入ダンパで、これを開けることにより新鮮
な空気が空気取入口21から導管8、処理槽1に送り込ま
れるようになっている。12は溶剤通路で、ドライクリー
ナの洗浄時には溶剤が満たされているが、脱水時には溶
剤はボタントラップ14を通り、更に管17を通り、ポンプ
15により溶剤フィルタ及び溶剤タンク(いずれも図示な
し)に送り出され、管内は空になる。16は溶剤用の切換
弁である。また13は溶剤通路12から吸気管3へ通じるバ
イパス管である。18は水分離器で、前記冷却器5,6で液
化して風路の下側に溜った溶剤や水が、管19を通って此
処に送られるようになっている。なお、ドライクリーナ
に活性炭吸着器を備えている場合は、排出口20は吸着器
に連結される。
Reference numeral 11 denotes an outside air intake damper, which is opened so that fresh air is sent from the air intake 21 to the conduit 8 and the processing tank 1. Reference numeral 12 denotes a solvent passage, which is filled with the solvent when the dry cleaner is washed, but the solvent passes through the button trap 14 and further through the pipe 17 during dehydration, and is pumped.
It is sent to a solvent filter and a solvent tank (both not shown) by 15 and the inside of the pipe becomes empty. Reference numeral 16 denotes a switching valve for a solvent. Reference numeral 13 denotes a bypass pipe that leads from the solvent passage 12 to the intake pipe 3. Numeral 18 denotes a water separator, in which the solvent and water liquefied by the coolers 5 and 6 and accumulated on the lower side of the air passage are sent through a pipe 19 to here. If the dry cleaner has an activated carbon adsorber, the outlet 20 is connected to the adsorber.

次に作用を説明する。先ず第1図の乾燥工程について
説明すると、前工程の脱液において溶剤通路12に溜めら
れていた溶剤及び処理ドラムの高速回転によって衣類よ
り振り切られた溶剤は、ボタントラップ14を通り、管17
を経て溶剤ポンプ15に吸出され、通路12は溶剤なしの状
態となっている。次いで乾燥工程になると、処理ドラム
はゆっくり回って衣類を程良くほぐし、送風機2によっ
て循環する空気を衣類に吹付ける。絞り弁9は開の位
置、切換弁10は排出口閉、導管8は開となっている。ま
た外気取入れダンパ11は空気取入口閉となっている。
Next, the operation will be described. First, the drying step in FIG. 1 will be described. In the previous step of dewatering, the solvent stored in the solvent passage 12 and the solvent shaken off from the clothes by the high-speed rotation of the processing drum pass through the button trap 14 through the pipe 17.
Through the solvent pump 15, and the passage 12 is in a state without solvent. Then, in the drying step, the processing drum slowly rotates to loosen the clothes appropriately, and blows the air circulated by the blower 2 onto the clothes. The throttle valve 9 is open, the switching valve 10 is closed, and the conduit 8 is open. The outside air intake damper 11 is closed.

送風機2によって送られる空気の流れは、矢印で示し
た如く処理槽1、吸気管3、リントフィルタ4、送風機
2、水冷却器5、冷媒冷却器6、加熱器7及び導管8を
循環する。また衣類に残っている溶剤は、吹付けられる
空気によって蒸発し、溶剤ガスの混った空気が水冷却器
5、冷媒冷却器6に達すると、溶剤は液化して導管の下
部に溜り、管19を通って水分離器18に送られる。ガスと
同時に水分を除かれた乾燥空気は、加熱器7により温風
となって再び処理槽内の衣類から溶剤を気化させて奪
う。この空気の循環の際に溶剤の混合した空気の一部
は、処理槽1の下部から溶剤通路12、バイパス管13を通
ってリントフィルタ4の手前において吸気管3を通る空
気の流れに合流する。溶剤の気化ガスは空気より2乃至
3倍重いので、この処理槽1下部からの吸い込みは効果
がある。この溶剤通路12、バイパス管13を通る空気をよ
り多くする為には、絞り弁9の開度を調節し、吸気管3
の空気通路を狭くしてやればよい。この工程を衣類が乾
燥するまで続ける。
The flow of air sent by the blower 2 circulates through the processing tank 1, the intake pipe 3, the lint filter 4, the blower 2, the water cooler 5, the refrigerant cooler 6, the heater 7 and the conduit 8, as indicated by arrows. The solvent remaining in the clothes evaporates by the air blown, and when the air containing the solvent gas reaches the water cooler 5 and the refrigerant cooler 6, the solvent liquefies and accumulates in the lower part of the conduit, and the pipe is removed. It is sent through 19 to a water separator 18. The dry air from which moisture has been removed at the same time as the gas is turned into warm air by the heater 7 to vaporize and take away the solvent from the clothes in the processing tank again. At the time of this air circulation, a part of the air mixed with the solvent flows from the lower part of the processing tank 1 through the solvent passage 12 and the bypass pipe 13 into the air flow passing through the suction pipe 3 in front of the lint filter 4. . Since the vaporized gas of the solvent is two to three times heavier than air, the suction from the lower part of the processing tank 1 is effective. In order to increase the amount of air passing through the solvent passage 12 and the bypass pipe 13, the opening of the throttle valve 9 is adjusted,
It is sufficient to make the air passage narrow. This process is continued until the clothes are dry.

次に第2図は脱臭工程における空気弁の働きと空気の
流れを示す。さて脱臭時の各空気弁の位置状態は、空気
取入口21の外気取入ダンパ11は開の位置、吸気管3の中
の絞り弁9は殆んど吸気管3を閉じる位置、切換弁10は
加熱器方向は風路を閉じ、排出口20は開くような状態に
位置する。従って新鮮な空気が取入口21から矢印の如く
処理槽1に吸込まれる。そして処理槽1内のドラムがゆ
っくり回って衣類を適当にほぐし、空気の流れに当てて
衣類に残った溶剤ガスは空気に奪い取られ、矢印の如く
処理槽1の下方から、通路12及びバイパス管13を通って
吸気管3の絞り弁9の後方に入り、リントフィルタ4、
送風風2を通り、水冷却器5、冷媒冷却器6で若干の溶
剤を液化した後の溶剤ガス濃度の薄くなった空気は、矢
印の如く排出口20から外気へ(又は活性炭吸着器へ)送
り出される。なお、この工程においては加熱器は使用し
ない。また水冷却器5、冷媒冷却器6で液化した溶剤
は、管19により水分離器18に送られ回収される。
Next, FIG. 2 shows the function of the air valve and the flow of air in the deodorizing step. The position of each air valve at the time of deodorization is as follows: the outside air intake damper 11 of the air intake 21 is in the open position, the throttle valve 9 in the intake pipe 3 is almost in the position to close the intake pipe 3, the switching valve 10 Is located in such a state that the air path is closed in the heater direction and the outlet 20 is open. Therefore, fresh air is sucked into the processing tank 1 from the inlet 21 as shown by the arrow. Then, the drum in the processing tank 1 rotates slowly to loosen the clothes appropriately, and the solvent gas remaining on the clothes is exposed to the flow of air and is taken away by the air. 13 and behind the throttle valve 9 of the intake pipe 3, the lint filter 4,
After passing through the blast air 2 and liquefying a small amount of the solvent in the water cooler 5 and the refrigerant cooler 6, the air having a reduced solvent gas concentration flows from the outlet 20 to the outside air (or to the activated carbon adsorber) as shown by the arrow. Will be sent out. Note that a heater is not used in this step. The solvent liquefied by the water cooler 5 and the refrigerant cooler 6 is sent to the water separator 18 by a pipe 19 and collected.

(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、従来装置は乾燥中は処理槽に循環する風路は面積が
大きく、長さが短く、空気抵抗は小さくて大きな風量を
送ることが出来た。しかし脱臭時の、装置の出口から活
性炭吸着装置に連結される時には、風路の面積は小さ
く、長さも長いので、大きな風量を送ることは出来なか
ったが、本発明では処理槽下部から吸出すため重いガス
の停滞を無くし、脱臭も溶剤ガスの回収も効率が良くな
り、処理時間を短縮し、衣類にガス臭気の残る欠点を解
消できる。因みに従来方法で脱臭した場合には、排出口
の位置でガス濃度を測定した結果、200ppm以下になるの
に10分以上を要したのに対し、本発明装置によると、3
分程度で脱臭が完了した。これは従来の処理槽内の空気
流が上方のショートパスが顕著であったことによる。
(Effect of the Invention) Since the present invention is configured as described in detail above, in the conventional apparatus, the air passage circulating in the processing tank during drying is large in area, short in length, small in air resistance, and large in air volume. Could be sent. However, at the time of deodorization, when connected to the activated carbon adsorption device from the outlet of the device, the area of the air passage was small and the length was long, so it was not possible to send a large air volume, but in the present invention, the air is sucked out from the lower part of the treatment tank Therefore, the stagnation of heavy gas is eliminated, the efficiency of deodorization and the recovery of solvent gas is improved, the processing time is shortened, and the disadvantage that gas odor remains in clothes can be eliminated. By the way, when deodorizing by the conventional method, as a result of measuring the gas concentration at the position of the discharge port, it took 10 minutes or more to become 200 ppm or less.
Deodorization was completed in about a minute. This is because the short path in which the air flow in the conventional processing tank was upward was remarkable.

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

第1図及び第2図は夫々本発明の実施例を示すドライク
リーニング装置における溶剤回収装置の乾燥工程及び脱
臭工程時のガス及び空気の流れを示すシステム図、第3
図は従来の溶剤回収装置を示すシステム図である。 図の主要部分の説明 1……処理槽 2……送風機 3……吸気管 4……リントフィルタ 5……水冷却器 6……冷媒冷却器 7……加熱器 8……導管 9……絞り弁 12……溶剤通路 13……バイパス管 20……排出口 21……空気取入口
FIGS. 1 and 2 are system diagrams showing the flow of gas and air during a drying step and a deodorizing step of a solvent recovery apparatus in a dry cleaning apparatus according to an embodiment of the present invention, respectively.
FIG. 1 is a system diagram showing a conventional solvent recovery device. Description of main parts in the drawing 1 ... treatment tank 2 ... blower 3 ... intake pipe 4 ... lint filter 5 ... water cooler 6 ... refrigerant cooler 7 ... heater 8 ... conduit 9 ... throttle Valve 12: Solvent passage 13: Bypass pipe 20: Outlet 21: Air inlet

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】処理槽からリントフィルタ、送風機、冷却
器及び加熱器を経て同処理槽に帰還する循環路を有する
ドライクリーニング装置において、同処理槽下部から処
理槽上部の空気吹出し用導管にバイパス導管を設けると
共に、同空気吹出し用導管に絞り弁を設け、乾燥工程で
は同絞り弁を開けて充分に空気を通し、脱臭工程では同
絞り弁を閉じることにより、空気は溶剤用の導管と前記
バイパス導管を通って前記リントフィルタ及び送風機へ
と流れるようにしたことを特徴とするドライクリーニン
グ装置の溶剤回収装置。
In a dry cleaning apparatus having a circulation path returning from a processing tank to a processing tank via a lint filter, a blower, a cooler, and a heater, a bypass is provided from a lower part of the processing tank to an air blowing conduit at an upper part of the processing tank. In addition to providing a conduit, a throttle valve is provided in the air blowing conduit, and in the drying step, the throttle valve is opened to allow sufficient air to pass therethrough, and in the deodorization step, the throttle valve is closed. A solvent recovery device for a dry cleaning device, characterized in that it flows to the lint filter and the blower through a bypass conduit.
JP2016073A 1990-01-29 1990-01-29 Solvent recovery equipment for dry cleaning equipment Expired - Lifetime JP2744665B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2016073A JP2744665B2 (en) 1990-01-29 1990-01-29 Solvent recovery equipment for dry cleaning equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016073A JP2744665B2 (en) 1990-01-29 1990-01-29 Solvent recovery equipment for dry cleaning equipment

Publications (2)

Publication Number Publication Date
JPH03221098A JPH03221098A (en) 1991-09-30
JP2744665B2 true JP2744665B2 (en) 1998-04-28

Family

ID=11906393

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016073A Expired - Lifetime JP2744665B2 (en) 1990-01-29 1990-01-29 Solvent recovery equipment for dry cleaning equipment

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Publication number Priority date Publication date Assignee Title
KR100345954B1 (en) * 1999-11-29 2002-08-01 주식회사 고려과학 A cooling device of a dyeing tester & a method

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JPH03221098A (en) 1991-09-30

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