JPS60236695A - Drycleaner - Google Patents

Drycleaner

Info

Publication number
JPS60236695A
JPS60236695A JP9329584A JP9329584A JPS60236695A JP S60236695 A JPS60236695 A JP S60236695A JP 9329584 A JP9329584 A JP 9329584A JP 9329584 A JP9329584 A JP 9329584A JP S60236695 A JPS60236695 A JP S60236695A
Authority
JP
Japan
Prior art keywords
solvent
water
separated
water separator
specific gravity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP9329584A
Other languages
Japanese (ja)
Inventor
初田 剛一
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.)
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Sanyo Denki Co 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 Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP9329584A priority Critical patent/JPS60236695A/en
Publication of JPS60236695A publication Critical patent/JPS60236695A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Sorption (AREA)

Abstract

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

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は塩素系の溶剤、例えはパークロルエチレン、ト
リクロルエタンを用いて洗浄を行なうドライクリーナに
関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a dry cleaner that performs cleaning using a chlorine-based solvent, such as perchlorethylene or trichloroethane.

(1=I) 従来技術 この種のドライクリーナは高価な溶剤を再利用して経費
を軽減すへ(、使用済みの溶剤を蒸留し、混入している
水を水分離器で比重差により分離し、排出゛し、もって
溶剤を回収してシ)る。以下、断る回収手段を備えた従
来一般のドライクリーナについて特開昭58−6729
0号公報を引用し1第2図及び第3図に基づいて説明す
る。
(1=I) Conventional technology This type of dry cleaner reuses expensive solvents to reduce costs (the used solvent is distilled and the water that is mixed in is separated by a water separator based on the difference in specific gravity). Then, drain it and collect the solvent. The following is a description of a conventional general dry cleaner equipped with a collection means that refuses to be collected.
This will be explained based on FIG. 1, FIG. 2, and FIG. 3, citing Publication No. 0.

(1)は洗濯槽、(2)は溶剤タンク、(3〉は給液ポ
ンプで、洗濯開始時には溶剤タンク(2)内の溶剤が、
給液ポンプ(3)により一方向弁(4)及び電磁方(5
)を通して洗濯N(1)に供給きれる。(6)はドレン
ポンプで、洗濯運転中はこのドレンポンプにより洗濯槽
(1)内の溶剤が一方向弁(7)及び電磁弁(5)を通
って循環する。(8〉は蒸留器で、仕切板(9)によっ
て蒸留室(lO)と加熱室(11)に区画されており、
二の加熱室内には電気ヒータ(12)が設けられ工いる
。(13)は加熱室(11)内の圧力を検出するだめの
圧力スイ/チである。この蒸留器(8)の使用時には上
記加熱室(11)内に水が入れられ、この水を上記電気
ヒータ(12)で加熱することによって蒸気を発生し、
この蒸気によって上記仕切板(9)を介して蒸留室(1
0)内の溶剤を加熱し蒸留を行う。
(1) is the washing tub, (2) is the solvent tank, and (3) is the liquid supply pump. When washing starts, the solvent in the solvent tank (2) is
The one-way valve (4) and the solenoid valve (5) are operated by the liquid supply pump (3).
) can be supplied to washing machine N(1). (6) is a drain pump, which circulates the solvent in the washing tub (1) through the one-way valve (7) and the solenoid valve (5) during washing operation. (8> is a distiller, which is divided into a distillation chamber (lO) and a heating chamber (11) by a partition plate (9),
An electric heater (12) is installed in the second heating chamber. (13) is a pressure switch for detecting the pressure inside the heating chamber (11). When using this distiller (8), water is put into the heating chamber (11), and steam is generated by heating this water with the electric heater (12),
This steam passes through the partition plate (9) into the distillation chamber (1).
0) is heated and distilled.

(14)は両端を上記洗濯室(1)に連通した乾燥通風
路で、該通風路内には、フィルタ(15)・フロートス
イッチ(16)・送風機(17)・凝縮器(18)・加
熱器(19〉が順に設けられている。尚、前記した洗濯
運転中は、上記フロートスイッチ(16)の位置までこ
の乾燥通風路(14)内にも溶剤が入り、このブロード
スイッチ(16)によって洗濯槽(1)内の溶剤液位が
制御される。又、上記加熱器(19)は蛇行状の熱媒通
路(19’)に多数の板状放熱フィンを嵌合した通常の
ラジェータ構造を有しており、上記熱媒゛通路(19’
)の一端はバルブ(2o)を介して上記蒸留器く8)に
接続し、他端は水分離器(21)に接続して、この水分
離器は更に上記溶剤タンク(2月こ接続している。一方
、凝縮器(18)の冷媒通路(18’)はその一端をつ
オータチラ〜の流出側(A)に接続し、他端側は上記水
分離器(21)内の冷却コイル(22〉及び溶剤タンク
(2)内の冷却コイル(23)を通してウォータテラー
流入側(B)に接続している。
(14) is a drying ventilation passage whose both ends communicate with the laundry room (1), and inside the ventilation passage there is a filter (15), a float switch (16), a blower (17), a condenser (18), a heating During the above-mentioned washing operation, the solvent enters the drying ventilation passage (14) up to the position of the float switch (16), and the broad switch (16) The solvent level in the washing tub (1) is controlled.The heater (19) has a normal radiator structure in which a number of plate-shaped heat dissipating fins are fitted into a meandering heat medium passage (19'). The heating medium passage (19'
) is connected to the distiller (8) through the valve (2o), and the other end is connected to the water separator (21), which in turn is connected to the solvent tank (21). On the other hand, one end of the refrigerant passage (18') of the condenser (18) is connected to the outflow side (A) of the water separator (21), and the other end is connected to the cooling coil (A) in the water separator (21). 22> and is connected to the water teller inlet side (B) through a cooling coil (23) in the solvent tank (2).

(24)は上記凝縮器(18)に於て凝縮した溶剤を回
収するための溶剤回収パイプで、回収液集合槽(25)
に一旦集めた後、電磁弁(26)を介して上記水分離器
(21)に流すようにしている。(27)(2g)は夫
々吸気弁と排気弁で、乾燥行程中は図の破線の位置にあ
って、乾燥通風路に設けた吸気口(29)と排気口(3
0)を閉じると共に、乾燥行程後の脱臭行程時には図の
実線位置に切換って、乾燥通風路(14)を遮断すると
同時に上記吸気口〈29)と排気口(30)を開放オる
。′(:i’l)は上記送風4m(17)を駆動するモ
ータである。
(24) is a solvent recovery pipe for recovering the solvent condensed in the condenser (18), and the recovered liquid collection tank (25)
Once collected, the water is sent to the water separator (21) via a solenoid valve (26). (27) (2g) are an intake valve and an exhaust valve, respectively. During the drying process, they are located at the position indicated by the broken line in the figure, and the intake port (29) and exhaust port (3
0), and during the deodorizing process after the drying process, the position is switched to the solid line position in the figure to block the drying ventilation path (14) and at the same time open the intake port (29) and the exhaust port (30). '(:i'l) is a motor that drives the air blower 4m (17).

以上の構成に於て、洗い行程及び脱液行程が終了すると
、乾燥行程に入ると同時に溶剤の蒸留が行われる。即ち
洗い行程が終了すると、ドレンポンプ(6)が回転して
、洗濯槽(1ン内の溶剤が電磁バルブ(32)を通して
蒸留室(10)に入る。脱液行程中も同様である。脱液
行程終了後乾燥行程に入ると蒸留器の電気し一タ(12
)に通電きれ、加熱室(11)内に蒸気を発生する。従
って、蒸留室(10)内に入った溶剤は上記蒸気に加熱
されて蒸発し、バルブ(20)を通っ℃加熱器(19)
に流入する。一方、この時には送風機(17)が回転す
ると共に、ウォータチラーから凝縮器(18)に冷水が
流れている。
In the above configuration, when the washing process and the deliquing process are completed, the solvent is distilled at the same time as the drying process begins. That is, when the washing process is completed, the drain pump (6) rotates, and the solvent in the washing tank (1 tank) enters the distillation chamber (10) through the electromagnetic valve (32). When the drying stage begins after the liquid stage is over, the distiller's electricity is turned on (12
) is turned off and steam is generated in the heating chamber (11). Therefore, the solvent that has entered the distillation chamber (10) is heated by the vapor and evaporates, passing through the valve (20) to the °C heater (19).
flows into. On the other hand, at this time, the blower (17) is rotating and cold water is flowing from the water chiller to the condenser (18).

従って、送風@(17)によって洗濯槽(18)から乾
燥通風路(14)内に吸引された空気は、凝縮器(18
)を通過する時にこの空気に含まれている溶剤を凝縮し
、この凝縮した溶剤は回収液集合jTII(25)に集
められ、乾燥行程終了後電磁弁(26〉が開いた時に水
分離器(21)に流れて、更に溶剤夕/り(2〉に回収
される。一方、凝縮器<18)を通過した空気は加熱器
(19〉を通過する。この加熱器(19)の熱媒通路(
19’)には、前述の如く蒸留器(8)から蒸発した高
温の溶剤蒸気が流れているので、この加熱器(19)は
高温になっている。従って、上記空気はこの加熱器(1
9)を通過する際に加熱され、熱風となって上記洗濯槽
(,1,)に吹田でこのfc濯槽内の衣類から溶剤を蒸
発させ、衣類の乾燥を行う。一方、上記加熱器の熱媒通
路(19’)を流れている溶剤蒸気は、この加熱器(1
9)に於て放熱することによって凝縮し、更に水分離器
(21)に流入する。水分離器(21)に入った溶剤は
、コイル(22)によって更に冷却され、且つ水を分離
した後溶剤タンク(2)に回収される。この乾燥行程は
蒸留が完了するまで継続する。即ちi省が完了して蒸留
室(10)内の溶剤が無くなると、加熱室(11〉内の
圧力が急上昇するので、それを圧力スイッチ(13〉が
検出して乾燥行程を終える。
Therefore, the air drawn into the drying ventilation passage (14) from the washing tub (18) by the air blower @ (17) is transferred to the condenser (18).
), the condensed solvent is collected in the collected liquid collection jTII (25), and when the solenoid valve (26> is opened after the drying process is completed, it is transferred to the water separator ( The air that has passed through the condenser (18) passes through the heater (19).The heating medium passage of this heater (19) (
The heater (19) is at a high temperature because the high temperature solvent vapor evaporated from the distiller (8) is flowing through the heater (19') as described above. Therefore, the above air is supplied to this heater (1
9), it is heated and turned into hot air, which evaporates the solvent from the clothes in the FC washing tub (,1,) and dries the clothes. On the other hand, the solvent vapor flowing through the heating medium path (19') of the heater (19')
The water is condensed by dissipating heat in step 9), and further flows into the water separator (21). The solvent that has entered the water separator (21) is further cooled by the coil (22), and after water is separated, it is collected in the solvent tank (2). This drying process continues until the distillation is complete. That is, when step i is completed and the solvent in the distillation chamber (10) is exhausted, the pressure in the heating chamber (11>) increases rapidly, which is detected by the pressure switch (13>) and the drying process is completed.

このようにして乾燥が終了すると脱臭行程に入る。脱臭
行程では吸気弁(27)と排気弁(28〉が図の実線位
置に切換って吸気口(29)と排気口(30)を開き、
吸気口(29)から洗濯槽(1)内に新鮮な空気を取入
れ、更に排気口<30)より排出する。これにより、乾
燥行程後も洗濯槽(1)内に充満していた溶剤蒸気は排
気口(30〉より排出される。
When drying is completed in this way, a deodorizing process begins. In the deodorizing process, the intake valve (27) and exhaust valve (28> are switched to the solid line position in the figure to open the intake port (29) and exhaust port (30),
Fresh air is taken into the washing tub (1) through the intake port (29) and is further discharged through the exhaust port (<30). As a result, the solvent vapor that had filled the washing tub (1) even after the drying process is discharged from the exhaust port (30>).

ここで、上記水分離器(21)は第3図で示すように、
器内に仕切板(33ンによって仕切られた溶剤収容室(
34)と分離室(35)を形成し、両室(34)(35
)間を仕切板(33)の下部で連通している。器体上部
には加熱器(19)、電磁弁(26)に連通ずる導入管
(36)が挿着きれ、溶剤収容室(34)の上部には溶
剤タンク(2)に連通ずる回収管(37〉が挿着きれ、
分離室り35)の上部には分離水の排出管(38)が挿
着しである。(39)は器内の臭気を乾燥通風路(14
〉内に放出する放出管である。そして、との水分離器(
21)は蒸留溶剤や凝縮器(18)によって凝縮された
溶剤を導入し、冷却し、分離室(35)内で比重の大小
によって水を分離する。比重の大きな溶剤は!剤数容室
(34〉に移動し、比重の小さな水は分離室(35)内
の上部に水層を作り、順次排出される。
Here, the water separator (21) is as shown in FIG.
There is a solvent storage chamber divided by a partition plate (33 mm) inside the container.
34) and a separation chamber (35), and both chambers (34) (35) are formed.
) are communicated at the lower part of the partition plate (33). An introduction pipe (36) that communicates with the heater (19) and the solenoid valve (26) can be inserted into the upper part of the container, and a recovery pipe (36) that communicates with the solvent tank (2) is installed in the upper part of the solvent storage chamber (34). 37〉 is fully inserted,
A separated water discharge pipe (38) is inserted into the upper part of the separation chamber 35). (39) is the ventilation passage (14) that dries the odor inside the vessel.
〉It is a discharge tube that discharges into the inside. And a water separator with (
21) introduces a distilled solvent or a solvent condensed by a condenser (18), cools it, and separates water according to its specific gravity in a separation chamber (35). Solvents with high specific gravity! Water with a low specific gravity forms an aqueous layer in the upper part of the separation chamber (35) and is sequentially discharged.

ところが、第4図(イ)(ロ)の特性図で明らかなよう
に溶剤は水中に溶解するので、排出水には溶剤が含まれ
る。また、溶剤は凝縮により大きな液滴にならないかぎ
り、比重差だけでは分離しきれず、水層中に微細なコロ
イド□状態で分散され、排出水中の溶剤含有率を溶解度
以上に上げる。更に、溶剤は大きな液滴にならない場合
は比重差よりも表面張力差の方が大きく作用しr水層面
上を止すへりし、そのまま排出管(38)から出ていく
ことがあった。こうして、排出された水は地下水等に混
入きれるが、塩素系溶剤が発ガン物質であることから排
出水中の溶剤を完全回収することが要望きれてきた。
However, as is clear from the characteristic diagrams in FIGS. 4(a) and 4(b), since the solvent is dissolved in water, the discharged water contains the solvent. Furthermore, unless the solvent condenses into large droplets, it cannot be completely separated by the difference in specific gravity alone, and is dispersed in the water layer in the form of a fine colloid, increasing the solvent content in the discharged water to a level higher than its solubility. Furthermore, if the solvent does not form into large droplets, the difference in surface tension acts more strongly than the difference in specific gravity, causing the solvent to stop on the surface of the water layer and exit from the discharge pipe (38) as it is. In this way, the discharged water can be mixed into underground water, etc., but since chlorinated solvents are carcinogenic substances, there has been a desire to completely recover the solvents in the discharged water.

(ハ) 発明の目的 本発明は分離され、排出される水から溶剤を極力分離除
去せんとするものである。
(c) Purpose of the Invention The present invention aims to separate and remove the solvent from the separated and discharged water as much as possible.

(二〉 発明の構成 本発明は、水分離器で比重差によって分離された水から
、活性炭等の吸着剤によって溶剤を吸着して分離するこ
とを特徴としたドライクリーナである。即ち、飽和濃度
以上に溶剤が含まれた場合は比重差たけでは分離できな
いところ、これらの分離水から溶剤を吸着除去し、排出
水中の溶剤濃度を零或いは著しく低減し、排出水による
地下水等の汚染を助士するものである。
(2) Structure of the Invention The present invention is a dry cleaner characterized in that a solvent is adsorbed and separated from water separated by a difference in specific gravity in a water separator using an adsorbent such as activated carbon. If a solvent is contained in the above water, it cannot be separated due to the difference in specific gravity, but the solvent is adsorbed and removed from the separated water, reducing the concentration of solvent in the wastewater to zero or significantly, and helping prevent contamination of groundwater, etc. by the wastewater. It is something.

(ホ)実施例 本発明の分離手段について第1図に基づいて説明するが
、ドライクリーナとしての溶剤回路は従来一般のものと
同様なので第2図を援用する。
(e) Embodiment The separation means of the present invention will be explained based on FIG. 1, but since the solvent circuit as a dry cleaner is the same as a conventional one, FIG. 2 will be referred to.

(40)は有底筒状の水分離器で、下部側壁に溶剤タン
ク(2)に屈曲路を経て連通ずる回収管<41)を連結
、連通し、上部側壁に分離すべき蒸留溶剤等の導入管(
42)を連結、連通し、底部中央には外部から内部上部
まで突入する分離水の一次排出管(43)を挿着してい
る。(44)は水分離器(40)の上部開口を密封する
蓋体で、下向きの筒(45)を−次排出管(43)を囲
むように深く垂設し、中心部には溶剤臭気の放出管(4
6)を連結、連通している。り47)は乾燥通風路(1
4)内に連通ずる連通管で、回収管(41)の屈曲路上
部と放出管(46)が連通している。
(40) is a cylindrical water separator with a bottom, the lower side wall is connected to a recovery pipe <41) which communicates with the solvent tank (2) via a bent path, and the upper side wall is used to collect distilled solvent, etc. to be separated. Introductory tube (
42) are connected and communicated with each other, and a primary discharge pipe (43) for separated water is inserted into the center of the bottom, which extends from the outside to the upper part of the inside. (44) is a lid body that seals the upper opening of the water separator (40), and a downward-facing cylinder (45) is vertically placed deeply so as to surround the secondary discharge pipe (43). Release tube (4
6) are connected and communicated. 47) is the drying ventilation passage (1
4), through which the upper part of the curved surface of the recovery pipe (41) and the discharge pipe (46) communicate.

(48)は有底筒状の溶剤鉄着器で、器体内のF部に格
子状或いは多孔状の載置棚(49)を配設し、この載置
棚(49)上に溶剤吸着剤とし℃の活性炭(50)を収
納し工いる。そして、上記吸着器(48)は底部に上記
−次排出管(43)を連結、連通ずると共に、+側壁に
下水道に連る二次排出管(51)を連結、連通している
。尚、(52)はドレンバルブ、(53)は蓋体である
(48) is a cylindrical solvent iron applicator with a bottom, and a lattice-like or porous mounting shelf (49) is arranged in the F part of the vessel, and a solvent adsorbent is placed on this shelf (49). Store and prepare activated carbon (50°C). The adsorber (48) connects and communicates with the secondary discharge pipe (43) at the bottom, and connects and communicates with the secondary discharge pipe (51) leading to the sewer on the positive side wall. In addition, (52) is a drain valve, and (53) is a lid body.

ここで、上記水分離器(40)と溶剤吸着器(48)は
桟(54)(54)によって連結されており、相互の高
さ位置が固定しである。そして、内器(40)(48>
間には水頭差が作ってあり、水分離器(40)から溶剤
吸着器(48)へ分離水が自動的に流出するようにしで
ある。
Here, the water separator (40) and the solvent adsorber (48) are connected by crosspieces (54) (54), and their height positions are fixed. And the inner device (40) (48>
A head difference is created between them so that separated water automatically flows from the water separator (40) to the solvent adsorber (48).

分離動作について説明すると、導入管(42)から水分
離器(40)内に導入きれた溶剤及び水は器内において
冷却器(図示せず)によって冷却され、その比重差によ
り下部に溶剤層を、上部に水層を夫々形成する。下部の
溶剤は回収管(41)から導出され、上部の水哄−次排
出管(43)から排出される。
To explain the separation operation, the solvent and water introduced from the introduction pipe (42) into the water separator (40) are cooled by a cooler (not shown) inside the vessel, and due to the difference in specific gravity, a solvent layer is formed at the bottom. , respectively forming a water layer on top. The solvent in the lower part is led out from the recovery pipe (41) and discharged from the upper part of the water bottle secondary discharge pipe (43).

この時にs <”45)は導入溶剤及び水と排出水との
混合を避けるた玩・の仕切壁を構成している。
At this time, s<45) constitutes a partition wall that prevents the introduced solvent and water from mixing with the discharged water.

比重差で分離されまた分離水は溶剤吸着器(48ンに、
、下部から水頭差によ□っ1自動流入し、活性炭(50
)” を通、過す゛る際に溶剤層がそこ、で吸着さパ、
二次IJト□出管(51〉から排出される。従って、排
出水中の溶剤濃度は零に或いは極め−(小さくなってい
る。
Separated water is separated based on the difference in specific gravity, and the separated water is separated using a solvent adsorber (48 ml).
, □1 automatically flows in from the bottom depending on the water head difference, and activated carbon
)”, the solvent layer is adsorbed there,
It is discharged from the secondary IJ outlet pipe (51). Therefore, the solvent concentration in the discharged water is zero or extremely small.

連通管(47)に出た溶剤蒸気、臭気は、溶剤回路にお
ける乾燥通風路(14)内に至り、ここで凝縮器(18
)によって凝縮され0回収液集合槽(25)に流れ、こ
こから再度導入管(42)を介して水分離器(40〉内
に導入きれ、上述の分離動作を繰返して実行される。
The solvent vapor and odor coming out of the communication pipe (47) reach the drying ventilation passage (14) in the solvent circuit, where they are transferred to the condenser (18).
) and flows into the zero recovery liquid collection tank (25), from where it is introduced into the water separator (40) again via the introduction pipe (42), and the above-described separation operation is repeated.

尚、活性炭(50)は予め袋づめされ又おり、適時交換
され、吸着した溶剤は適当な手段で回収される。
Incidentally, the activated carbon (50) is packed in a bag in advance and is replaced from time to time, and the adsorbed solvent is recovered by appropriate means.

(へ)発明の効果 本発明に依れば、比重差では分離できない溶剤を吸着剤
により二次的に分離するので、排出水中の溶剤濃度を零
に或いは著しく低減でき、外部の地下水等の汚染を未然
に防止する高性能なドライクリーナを提供できるもので
ある。
(F) Effects of the Invention According to the present invention, since the solvent that cannot be separated based on the difference in specific gravity is secondarily separated using an adsorbent, the concentration of the solvent in the discharged water can be reduced to zero or significantly, thereby preventing contamination of external groundwater, etc. It is possible to provide a high-performance dry cleaner that prevents this from occurring.

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

第1図は本発明によるドライクリーナの分離手段を示す
断面機構図、第2図は従来一般のドライクリーナの溶剤
回路図、第3図は従来の分離手段の断面図、第4図(イ
)く口〉は水と溶剤の溶解度を示す特性図である。 (40〉・・水分離器、(48〉・・溶剤吸着器、(5
0)・・・活性炭。 出願人 三洋電機株式会社 代理人 弁理士 佐野靜夫 第1図 第2図 =] 第3図 9 (%V峰ダ9!事1)1鉤蕃ざ□
Fig. 1 is a sectional mechanical diagram showing the separating means of a dry cleaner according to the present invention, Fig. 2 is a solvent circuit diagram of a conventional dry cleaner, Fig. 3 is a sectional view of the conventional separating means, and Fig. 4 (A). 〉 is a characteristic diagram showing the solubility of water and solvent. (40>・Water separator, (48>・Solvent adsorption device, (5
0)...Activated carbon. Applicant Sanyo Electric Co., Ltd. Agent Patent Attorney Shizuo Sano Figure 1 Figure 2 =] Figure 3 9 (%V peak da 9! thing 1) 1 hook □

Claims (1)

【特許請求の範囲】[Claims] (1)洗浄に用いられた塩素系の溶剤を蒸宿しで回収す
るドライクリーナに於いて、蒸留溶剤中の水を比重差で
分iする水分離器k、分離水から溶剤を活性炭等の吸着
剤によって分離する溶剤吸着器とを備えたことを特徴と
するドライクリーナ。
(1) In dry cleaners that recover chlorinated solvents used for cleaning by steaming, a water separator k separates the water in the distilled solvent based on the difference in specific gravity, and a water separator k separates the water from the separated water using activated carbon, etc. A dry cleaner characterized by comprising a solvent adsorber that separates using an adsorbent.
JP9329584A 1984-05-10 1984-05-10 Drycleaner Pending JPS60236695A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9329584A JPS60236695A (en) 1984-05-10 1984-05-10 Drycleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9329584A JPS60236695A (en) 1984-05-10 1984-05-10 Drycleaner

Publications (1)

Publication Number Publication Date
JPS60236695A true JPS60236695A (en) 1985-11-25

Family

ID=14078377

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9329584A Pending JPS60236695A (en) 1984-05-10 1984-05-10 Drycleaner

Country Status (1)

Country Link
JP (1) JPS60236695A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0577563A1 (en) * 1992-05-14 1994-01-05 Renzacci S.P.A. Industria Lavatrici Method and apparatus for the removal of residues of chlorinated solvent from contact waters formed during the drying stage in machines for the dry-cleaning of garments

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0577563A1 (en) * 1992-05-14 1994-01-05 Renzacci S.P.A. Industria Lavatrici Method and apparatus for the removal of residues of chlorinated solvent from contact waters formed during the drying stage in machines for the dry-cleaning of garments

Similar Documents

Publication Publication Date Title
US4513590A (en) Combination filter apparatus for use with a dry cleaning machine
US4056369A (en) Method of and apparatus for the recovery of a desired material from a carrier stream
WO2003089709A2 (en) Apparatus and method for article cleaning
WO2006054408A1 (en) Distillation apparatus for dry cleaner
US3274755A (en) Apparatus for the adsorptive recovery of solvents
US4817296A (en) Dry-cleaning machine for textiles
JPS60236695A (en) Drycleaner
JPS60236694A (en) Drycleaner
FI79864C (en) FOERFARANDE FOER AOTERVINNING AV LOESNINGSMEDEL VID BEHANDLING AV TEXTILIER.
JPS5865199A (en) Dry cleaner
JPS6340118B2 (en)
JPH0422811Y2 (en)
JP3082787B2 (en) Dry cleaning machine
JPS601778Y2 (en) filtration device
JP2792705B2 (en) Solvent recovery equipment for dry cleaning equipment
JP2587075Y2 (en) Dry cleaner solvent cooling system
JPH0639670Y2 (en) Solvent recovery device
JPS6143434Y2 (en)
JPS6320081A (en) Moving type steam wahser
JPS5818874Y2 (en) dry cleaner
JPS6345275Y2 (en)
JP2590729Y2 (en) Activated carbon solvent recovery equipment with hot air desorption
JPS6321289Y2 (en)
JPS6329517Y2 (en)
JPH0224560B2 (en)