JPS59179872A - Drying of washed article in dry cleaner - Google Patents

Drying of washed article in dry cleaner

Info

Publication number
JPS59179872A
JPS59179872A JP5477683A JP5477683A JPS59179872A JP S59179872 A JPS59179872 A JP S59179872A JP 5477683 A JP5477683 A JP 5477683A JP 5477683 A JP5477683 A JP 5477683A JP S59179872 A JPS59179872 A JP S59179872A
Authority
JP
Japan
Prior art keywords
drying
solvent
dry cleaner
tank
dry
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
JP5477683A
Other languages
Japanese (ja)
Inventor
哲三 山田
杉山 守男
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 JP5477683A priority Critical patent/JPS59179872A/en
Publication of JPS59179872A publication Critical patent/JPS59179872A/en
Pending legal-status Critical Current

Links

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】 本発明はパークロルエチレン、/、/、/  )リクロ
ルエタン、R/13などの有機溶剤を使用するドライク
リーニング機械における洗濯物の乾燥方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for drying laundry in a dry cleaning machine using organic solvents such as perchlorethylene, /, /, / )lychloroethane, R/13, etc.

一般的なドライクリーナ2示す第1図を用いて従来のド
ライクリーニング工程を概説すると先ずドア(1)から
衣料(コ)を投入する。そしてドア(1)を閉じて運転
を開始すると、一般には次の順序で工程が進行する。
To outline the conventional dry cleaning process using FIG. 1 showing a general dry cleaner 2, clothes (1) are first put in through the door (1). When the door (1) is closed and the operation is started, the steps generally proceed in the following order.

■ 溶剤タンク(3)から溶剤<ti>をバルブ(S)
を介してポンプ(A)で汲揚げ、バルブ(り)、フィル
タ(g)から成る経路またはバルブ(9)から成る経路
によって処理槽(/のに溶剤(’I)を必要量送り込む
■ Pour the solvent <ti> from the solvent tank (3) through the valve (S).
The required amount of solvent ('I) is pumped up by a pump (A) through the treatment tank (/) through a path consisting of a valve (ri) and a filter (g) or a path consisting of a valve (9).

■ 処理ドラム(//)をゆっくり回し、溶剤(グ)を
処理槽(lの、ボタントラップ(7,2)、バルブ(/
3)、ポンプ′(乙)、バルブ(7)、フィルり(g)
、!たは:   バルブ(9)から成る回路で循環して
衣料(コ)を洗浄する。
■ Slowly rotate the processing drum (//) and pour the solvent (g) into the processing tank (L), button trap (7, 2), and valve (//).
3), pump' (O), valve (7), fill (g)
,! Or: Clothes are washed by circulation through a circuit consisting of a valve (9).

■ 処理ドラム(//) 、ボタントラップ(/2) 
、バルブ(/、l) 、ポンプ(A)、バルブ(/lI
)、溶剤加熱慴(/S)の経路で排液し・つづいて処理
ドラム(l/)が高速回転して衣料(コ)中の溶剤(’
I)を遠心分離し、同様に排液する。
■ Processing drum (//), button trap (/2)
, valve (/, l), pump (A), valve (/lI
), the solvent is drained through the solvent heating tank (/S), and then the processing drum (l/) rotates at high speed to remove the solvent (') in the clothing.
Centrifuge I) and drain in the same manner.

■ 前記の項、0項の工程を繰り返えす。■ Repeat the steps in section 0 above.

■ 処理槽Cl/) 、ボタントラップCD) 、バル
ブ(13)、バルブ(S)の経路で溶剤タンク(3)に
排液し、つづいて処理ドラム(/l)が高速回転して衣
料(,2)中の溶剤悴)を遠心分離し、排液する。
■ The liquid is drained into the solvent tank (3) through the processing tank Cl/), button trap CD), valve (13), and valve (S), and then the processing drum (/l) rotates at high speed to remove the clothing (, 2) Centrifuge and drain the solvent.

■ 再び処理ドラム(l/)をゆっくり回し、ファン(
/A) 、エアクーラ(/7) 、エアヒータ(ig)
から成るリカバリエアダクl−(/9)と処理槽(10
)の間を矢印(曜〕の向きでエアを循環し、衣料(2)
を乾燥する。また衣料−)から蒸発した溶剤ガスは、エ
アクーラ(/2)で凝縮され5、回収経路(2/)を経
て水分離器(aユ)に入り、溶剤配管(U)を通ってタ
リンタンク(λダ)に入る。
■ Slowly turn the processing drum (l/) again and turn on the fan (
/A), air cooler (/7), air heater (ig)
A recovery air duct consisting of l-(/9) and a treatment tank (10
) Air is circulated in the direction of the arrow (Yo) between the clothing (2)
Dry. In addition, the solvent gas evaporated from the clothing (clothes) is condensed in the air cooler (/2), enters the water separator (ayu) via the recovery route (2/), passes through the solvent pipe (U), and then passes through the Tallinn tank (5). λda).

■ 乾燥が終了すると、ダンパ(B)(Ω6)が破線の
如く開き、同ダンパから新鮮な空気をとり入れて、ダン
パしA)からエアクーラ(/7〕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 drying is completed, damper (B) (Ω6) opens as shown by the broken line, and fresh air is taken in from the damper, and uncondensed solvent gas that cannot be recovered by the air cooler (/7) is exhausted from damper A). Deodorizes solvent odor in clothing (2).

■ 前記0項の工程で溶剤加熱槽(/左)に入った溶剤
(りは、蒸発して溶剤蒸気冷却回収部(2?)にて凝縮
回収され、水分離器(−二)、溶剤配管〔23〕′?i
:通ってタリンタンク(2’l)に入り、オーバフロー
付仕切板(2g)から溶剤タンク(3)に戻る。なお、
水分離器(ユニ)で分離した水は、水配管〔29〕によ
って系外へ排出する。
■ The solvent that entered the solvent heating tank (/left) in the process of item 0 above is evaporated, condensed and recovered in the solvent vapor cooling and recovery section (2?), and then transferred to the water separator (-2) and the solvent piping. [23]′?i
: Enter the Talin tank (2'l) and return to the solvent tank (3) through the overflow partition plate (2g). In addition,
The water separated by the water separator (UNI) is discharged out of the system through the water pipe [29].

次に第2図を用いて従来の蒸留器の作用および欠点を説
明する。従来の蒸留装置は溶剤加熱槽(/S)内に排液
された溶剤を、水蒸気式ヒータまたは電気式ヒータ(3
ユ)により加熱して気化させ、気化した溶剤蒸気は立昇
り管(3Q)を経て溶剤蒸気冷却回収部(λ7)に導ひ
かれ、ここで冷却水の流nる冷却コイル(31)によっ
て冷却さn1凝緬回収されていた。冷却水は溶剤蒸気冷
却後は廃棄されていた。
Next, the functions and drawbacks of the conventional distiller will be explained using FIG. In conventional distillation equipment, the solvent drained into the solvent heating tank (/S) is heated by a steam heater or an electric heater (3
The vaporized solvent vapor is led to the solvent vapor cooling and recovery section (λ7) through the riser pipe (3Q), where it is cooled by a cooling coil (31) through which cooling water flows. n1 was recovered. Cooling water was discarded after solvent vapor cooling.

ところで、従来の蒸留装置には次のような欠点があった
。先ず水蒸気加熱方式の場合は、ドライクリーナ装置と
は別に、ボイラ等の蒸気発生設備および蒸気配管等の設
備、蒸気ドレンの排水設備等が必等であった。また電気
ヒータ加熱方式の場合は、溶剤加熱コストが高かった。
However, conventional distillation apparatuses have the following drawbacks. First, in the case of the steam heating method, in addition to the dry cleaner device, steam generation equipment such as a boiler, equipment such as steam piping, drainage equipment for steam drain, etc. are required. Furthermore, in the case of the electric heater heating method, the cost of heating the solvent was high.

更に冷却水が溶剤蒸気冷却後廃棄されるため、排水設備
が必要であると共に、不経済であった。
Furthermore, since the cooling water is discarded after cooling with solvent vapor, drainage equipment is required and it is uneconomical.

一方乾燥において洗い上り衣料に発生する輪じみについ
ての恒久対策が、従来も強く要望されていた。
On the other hand, there has been a strong demand for permanent measures against the ring stains that occur on washed clothes during drying.

そこで本発明は、簡単な方法により輪じみ生成割合を低
減できる等の効果を奏する乾燥方法を得ようとするもの
で、ドライクリーナの乾燥工程において、低温による一
次乾燥を行ない、続いて高温の二次乾燥を行なうことに
より、乾燥速度の最も大きい表面、と幾分小さい周辺部
、内部間との乾燥速度斑を少なくして、布地内残液の浸
透、移行を極力抑制し、残液中の油脂の汚れ分などが表
面近傍に局部集中することなく、布地内に広く分散す′
ることを狙った洗濯物の乾燥方法を提供せんとするもの
である。
Therefore, the present invention aims to provide a drying method that is effective in reducing the rate of ring formation using a simple method.In the drying process of a dry cleaner, primary drying is performed at low temperature, followed by secondary drying at high temperature. By performing the next drying, the drying speed unevenness between the surface where the drying speed is the highest, the peripheral area where the drying speed is somewhat smaller, and the inside area is reduced, and the penetration and migration of the residual liquid in the fabric is suppressed as much as possible, and the residual liquid in the fabric is Oil and fat stains are dispersed widely within the fabric without concentrating locally near the surface.
The purpose of this invention is to provide a method for drying laundry.

そして前記方法によると、溶剤ロス、布地の仕上り時の
風合等の面で従来の熱風乾燥法に比べて何ら見劣りする
ことがない上、ラボ試験によれば輪じみ生成割合が3s
〜りθ%程度低減できる等の効果が得られた。
According to the above method, there is no inferiority in terms of solvent loss, finished texture of the fabric, etc. compared to the conventional hot air drying method, and according to laboratory tests, the rate of ring bleeding is 3 seconds.
Effects such as being able to reduce the loss by about θ% were obtained.

ドライクリーナ洗浄法は、もともと羊毛、絹製品など高
級天然衣料の洗い上り時のしわ、縮みなどの虞れのある
衣料を対象に行なわれて来たが、近年繊維製品の多様化
に伴い、殆どすべての素材衣料がその対象となっている
。ところで、ドライクリーニングは高価な有機系溶剤(
石油系、塩素系、弗素系溶剤など)を洗液とする関係か
ら、これ全回収して反復使用しなければならない等制約
があるため、溶剤中での油脂の汚れ分等の蓄4に1溶剤
劣化、すすぎの難かしさなど、逆汚染、輪じみの生成な
ど布地の洗い上り時の品質面からみると、ドライクリー
ナ特有のマイナス面があると言えよう。
The dry cleaner cleaning method was originally used for high-quality natural clothing such as wool and silk products that are prone to wrinkles and shrinkage after washing, but in recent years, with the diversification of textile products, it has been applied to almost all This applies to clothing made of materials. By the way, dry cleaning uses expensive organic solvents (
Because the cleaning fluid is a petroleum-based, chlorinated, fluorinated solvent, etc., there are restrictions such as having to collect all of it and use it repeatedly. Dry cleaners have their own downsides in terms of quality when cleaning fabrics, such as solvent deterioration, difficulty in rinsing, reverse contamination, and the formation of ring marks.

ところで輸じみ生成原因は、大別して下記コ項目に要約
できる。先ず高沸点の油脂、汚れ、洗剤などの洗液中で
の蓄積、濃度アップと、衣料中残液不足、ならびに乾燥
工程での乾燥斑の発生である。
By the way, the causes of blemish formation can be broadly classified into the following items. First, there is the accumulation and concentration increase of high-boiling point oils, dirt, detergents, etc. in the washing liquid, the lack of residual liquid in the clothes, and the occurrence of dry spots during the drying process.

このうち前者の原因は定期的なフィルタの点検、交換や
、適正な液管理など、ユーザサイドでの管理面に主体性
のあるものであるため、ここでは後者の原因について装
置面から検討を行なう。一般にドライクリ〜すでの洗浄
衣料の脱液、乾燥機牌を考えてみると、通常の固体(紙
、プラスチックスフィルム、シート類など〕の乾燥機購
と同様に、表面蒸発による恒率乾燥と、減率第1段、同
第2段という3段階の工程を経て進行するものと考えら
れる。
Of these, the former cause is dependent on user management, such as regular filter inspection and replacement, and proper liquid management, so here we will examine the latter cause from the equipment perspective. . Generally speaking, if we consider dry cleaning and drying of washed clothes, it is similar to the drying process of ordinary solids (paper, plastic film, sheets, etc.), and constant rate drying due to surface evaporation. It is thought that the process proceeds through three stages: , the first stage of reduction rate, and the second stage of reduction rate.

ところで実用時の乾燥条件をみると、洗浄衣料は脱液後
直ちにtQ’Qの熱風乾燥に付されており、その乾燥機
構を単純化して考えると、前記工程に準じた形で行わn
ていると見做される。
By the way, looking at the drying conditions in practical use, washed clothes are immediately subjected to hot air drying for tQ'Q after dehydrating, and if we consider the drying mechanism in a simplified manner, it is said that the drying process is carried out in a manner similar to the above process.
It is considered that

即ち、乾燥速度の最も大きい表面から残液の蒸発が先づ
行なわわ、引続いて衣料内部からその面への残液の浸透
、移行が行なわれ、油脂、汚れ分等は表面付近に局部集
中して輪じみの原因となっている。
In other words, the residual liquid evaporates first from the surface where the drying rate is highest, and then the residual liquid permeates and migrates from the inside of the clothing to that surface, and oils, fats, dirt, etc. are locally concentrated near the surface. This causes ring smearing.

そこで本発明では、脱液後の衣料を直接10Cの加熱乾
燥をTテなう前に、/!;−aOCの低温乾燥を5〜7
分間行ない、引続いて乙OCの熱風乾燥を行なうことを
特徴とするもので、こt’L[より以下の効果が期待さ
れる。
Therefore, in the present invention, before directly heating and drying the dehydrated clothing at 10C, /! ;-low temperature drying of aOC for 5 to 7
It is characterized by drying with hot air for 1 minute, followed by hot air drying.The following effects are expected.

即ち、本発明によると、乾燥速度の最も大きい乾燥初期
の段階で比較的ゆっくり乾燥が行なわれるため、蒸発表
面と内部、周辺部間の残液率の差は60C乾燥の場合に
比して少なくなる。
That is, according to the present invention, since drying is performed relatively slowly in the initial drying stage where the drying rate is highest, the difference in residual liquid ratio between the evaporation surface, the interior, and the peripheral area is smaller than in the case of 60C drying. Become.

移行がかなり抑制され、残液中の油脂分など輪じみの主
因となる有機物質は、乾燥速度の大きい表面のみに局部
集中することなく広い部分に分散するため、輪じみの現
われる割合が減少することになる。ただ、不十分な乾燥
のままでは、仕上り時の風合、溶剤ロス、廃ガス中の溶
剤濃度アップ等への影響が懸念さnるため、残液の移動
量の少なくなった時点、つまり5〜7分間の低温乾燥後
、通常のAOCの熱風乾燥を/S〜、20分程度行ない
完全乾燥して仕上げる。
Migration is considerably suppressed, and the organic substances that are the main cause of ring stains, such as oil and fat in the residual liquid, are dispersed over a wide area rather than being locally concentrated only on the surface where the drying rate is high, reducing the proportion of ring stains that appear. It turns out. However, if the drying process is insufficient, there are concerns that it will affect the texture of the finished product, solvent loss, increase in solvent concentration in the waste gas, etc. After low temperature drying for ~7 minutes, normal AOC hot air drying is performed for ~20 minutes to complete drying.

以下史に本発明?下記具体例により詳述する。This invention in history? This will be explained in detail using the following specific example.

実施例 条  件 ’ OCm平方の標準試験布を用い、下記の標準条件下
での洗浄、脱液、乾燥試験を行ない、乾燥刃θξの違い
による輪じみの出来具合を調べた。
Example Conditions Using a standard test cloth of OCm square, washing, deliquid, and drying tests were carried out under the following standard conditions, and the degree of ring smearing due to differences in the drying blade θξ was investigated.

(試験条件) /  標準試験布 (生地):(羊毛子キュプラ)一枚
の縫い合わせ布 Cサイズ):10crr+平方 −2洗 Kl:バークロルエチレンK O,5Vo1%
の非イオン系界面活性剤添加。
(Test conditions) / Standard test cloth (Fabric): (wool cupra) one piece of sewn cloth C size): 10 crr + square - 2 washes Kl: Verchlorethylene K O, 5 Vo 1%
Addition of nonionic surfactant.

3 脱 液:遠心式脱水槽(脱水容置λコkq )を利
用。
3. Dehydration: Use a centrifugal dehydration tank (dehydration tank λ).

l 乾 燥:の熱風乾燥(ZθC熱風×30分)(従来
法)。
l Drying: hot air drying (ZθC hot air x 30 minutes) (conventional method).

■低湿乾燥(/j−一〇’CX!i〜7分〕、後、熱風
乾燥(AO’Q熱 風X/j’−,20分)(本発明法〕。
■Low humidity drying (/j-10'CX!i~7 minutes), followed by hot air drying (AO'Q hot air X/j'-, 20 minutes) (method of the present invention).

S 洗浄機:イワキ製KM式加振器。S Cleaning machine: Iwaki KM type vibrator.

結  果 なお、本試験では輪じみ生成程1yは、しみ部面積の大
きさから評価した。
Results In this test, the degree of ring bleed formation 1y was evaluated from the size of the stained area.

前記試験により乙OC熱風乾燥と低湿乾燥(局部的に冷
風吹付けを行なった。)とで、じみの出来力を比較する
と・後者の方がしみ部面積で約グθ%程度低減できるこ
とが明らかになった。こねは低温乾燥が熱風乾燥に比べ
乾燥速度が遅く、しかも局部的表面乾燥であるため、布
地内での残液の浸透・移行(内部、周辺部→表面)がか
なり抑制され、輪じみの基となる残液中の油脂分などが
乾燥の速い表面部分に局部集中することなく、布地全域
に広く分散した結果と解釈される。
In the above test, when we compare the smudge production between Otsu OC hot air drying and low humidity drying (locally blown cold air), it is clear that the latter can reduce the smudge area by about 9%. Became. Low-temperature drying has a slower drying speed than hot-air drying, and since it only dries the surface locally, the penetration and migration of residual liquid within the fabric (from the inside and periphery to the surface) is considerably suppressed, and the basis of ring smudges. This is interpreted as a result of the oils and fats in the remaining liquid being dispersed widely over the entire fabric, rather than being locally concentrated on the surface area where it dries quickly.

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

第1図は従来のドライクリーナのシステム図、第2図は
第1図における要部の詳細図、第3図は本発明と従来法
との輪じみ部面積を比較する線図である。 特許用1幀人  三菱重工業株式会社
FIG. 1 is a system diagram of a conventional dry cleaner, FIG. 2 is a detailed view of the main parts in FIG. 1, and FIG. 3 is a diagram comparing the area of the ring portion of the present invention and the conventional method. 1 person for patent Mitsubishi Heavy Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] ドライクリーナの乾燥工程において、低温による一次乾
燥を行ない、続いて高温の二次乾畑を行なうことを特徴
とするドライクリーナにおける洗濯物の乾燥方法。
A method for drying laundry in a dry cleaner, characterized in that in the drying process of the dry cleaner, primary drying is performed at a low temperature, followed by secondary drying at a high temperature.
JP5477683A 1983-03-30 1983-03-30 Drying of washed article in dry cleaner Pending JPS59179872A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5477683A JPS59179872A (en) 1983-03-30 1983-03-30 Drying of washed article in dry cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5477683A JPS59179872A (en) 1983-03-30 1983-03-30 Drying of washed article in dry cleaner

Publications (1)

Publication Number Publication Date
JPS59179872A true JPS59179872A (en) 1984-10-12

Family

ID=12980170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5477683A Pending JPS59179872A (en) 1983-03-30 1983-03-30 Drying of washed article in dry cleaner

Country Status (1)

Country Link
JP (1) JPS59179872A (en)

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