JPH038863A - Method and device for treating cloth with steam - Google Patents

Method and device for treating cloth with steam

Info

Publication number
JPH038863A
JPH038863A JP14015789A JP14015789A JPH038863A JP H038863 A JPH038863 A JP H038863A JP 14015789 A JP14015789 A JP 14015789A JP 14015789 A JP14015789 A JP 14015789A JP H038863 A JPH038863 A JP H038863A
Authority
JP
Japan
Prior art keywords
steam
air
fabric
pipes
wound layer
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.)
Granted
Application number
JP14015789A
Other languages
Japanese (ja)
Other versions
JPH059538B2 (en
Inventor
Tadashi Muto
正 武藤
Takeshi Takada
健 高田
Masahiko Kamiyama
神山 征彦
Kan Otsu
大津 完
Masahiro Sawamura
澤村 政廣
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.)
Kanebo Ltd
Original Assignee
Kanebo 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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP14015789A priority Critical patent/JPH038863A/en
Publication of JPH038863A publication Critical patent/JPH038863A/en
Publication of JPH059538B2 publication Critical patent/JPH059538B2/ja
Granted legal-status Critical Current

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  • Treatment Of Fiber Materials (AREA)

Abstract

PURPOSE:To uniformly set a cloth wound layer with steam by discharging air in an oven having the cloth wound layer therein with a vacuum pump, allowing steam to pass through the cloth wound layer to substrate remained air with the steam and subsequently injecting steam into the cloth wound layer from both the inner and outer sides thereof. CONSTITUTION:A cloth wound layer 4 is mounted in a steam oven 1 and the steam oven 1 is closed. Valves 7, 8 and 14 are closed and valves 10, 11, 12 and 13 are opened, followed by actuating a vacuum pump 16 to discharge air in the oven 1. the valves 11 and 13 are subsequently closed and the valve 8 is opened to charge steam into the oven 1 from a steam supply source 9 through a stream pipe 5 and subsequently discharge the steam outside the oven 1 through the cloth wound layer 4 and a small diameter piping D, thereby maintaining the inner portion of the cloth wound layer 4 at a lower temperature than a prescribed temperature and substituting the remaining air with the stream. The valves 10 and 12 are closed and the vacuum pump 16 is stopped. The valves 7 and 8 are subsequently opened to inject the steam into the cloth wound layer 4 from both the inner and outer sides thereof for the treatment of the cloth wound layer 4 at a prescribed temperature for a prescribed time.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、布帛の蒸気処理工程における蒸気処理方法及
び蒸気処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a steam treatment method and a steam treatment apparatus in a fabric steam treatment process.

〔従来の技術〕[Conventional technology]

毛織編物2毛−合繊混繊編物の布帛には、仕上加工工程
にて寸法安定性や風合、光沢を向上させるために蒸気処
理を施すことが一般的である。
BACKGROUND ART Woolen knitted fabrics, bi-wool-synthetic fiber mixed knitted fabrics are generally subjected to steam treatment in order to improve dimensional stability, texture, and gloss in the finishing process.

この蒸気処理は、通常第3図に示すような蒸気釜(1)
内で行われる。即ち、被処理布帛は、蒸気釜(1)外で
予めラッピングクロスと呼ばれる綿布と面圧をかけて重
ね合わされながら多数の蒸気噴出孔(3)を有するシリ
ンダー(2)に巻き込まれて巻き層(4)に形成され、
蒸気釜(1)内に装填される。このときシリンダー(2
)の開放されている端(2a)は、蒸気供給源(9)及
び真空ポンプ(16)に夫々所定のバルブを介して連通
されている。また、蒸気釜(1)内には多数の蒸気噴出
孔(6)を有する蒸気バイブ(5)が挿入されていて、
その開放端(5a)は蒸気供給#(9)及び真空ポンプ
(16)に夫々所定のバルブを介して連通されている。
This steam treatment is usually carried out using a steam pot (1) as shown in Figure 3.
It is done within. That is, the fabric to be treated is overlapped with a cotton cloth called a wrapping cloth in advance by applying surface pressure outside the steam pot (1), and then rolled into a cylinder (2) having a large number of steam ejection holes (3) to form a wrapped layer ( 4) is formed,
It is loaded into the steam kettle (1). At this time, the cylinder (2
) is connected to a steam supply source (9) and a vacuum pump (16) via predetermined valves, respectively. Furthermore, a steam vibrator (5) having a large number of steam ejection holes (6) is inserted into the steam pot (1).
Its open end (5a) is communicated with a steam supply # (9) and a vacuum pump (16) via respective predetermined valves.

然して、供給源(9)から供給される蒸気が、バルブ(
7)からシリンダー(2)に入りその噴出孔(3)を通
って巻きN(4)の芯部から外表部へ流通するか、ある
いはバルブ(8)を経て蒸気パイプ(5)の蒸気噴出孔
(6)から釜(1)内に送入され巻き層(4)の外表部
から芯部へ流通することにより巻き層(4)の加熱が行
われるのである。
However, the steam supplied from the supply source (9) passes through the valve (
Steam enters the cylinder (2) from the cylinder (2) through its nozzle (3) and flows from the core of the winding N (4) to the outer surface, or passes through the valve (8) to the steam nozzle of the steam pipe (5). (6) into the pot (1) and flows from the outer surface of the wound layer (4) to the core, thereby heating the wound layer (4).

しかしながら、このような方法では巻き層(4)内、即
ち外表部と芯部との温度分布が不均一となD、布帛に対
して不均一な処理を施すことを免れなかった。
However, in such a method, the temperature distribution within the wound layer (4), that is, between the outer surface portion and the core portion is non-uniform, resulting in non-uniform treatment of the fabric.

そこで、布帛に均一な蒸気処理を施すことを目的として
様々な開発が進められた中に、特公昭47−42547
号公報に記載された蒸気処理方法等がある。これは断熱
圧縮による加熱方法を適用したものであって、1気処理
工程を、(ア)布帛内及び蒸気釜内空気を減少させる前
真空工程と、 (イ)蒸気セット温度より低い温度にて蒸気と残留空気
との置換を行う蒸気浸透工程と、(つ)蒸気を積極的に
流通せしめる蒸気送入及びセント工程と、 (1)蒸気排出工程、の4工程で構成したものである。
Therefore, various developments were carried out with the aim of applying uniform steam treatment to fabrics, and among them,
There is a steam treatment method described in the above publication. This is a heating method using adiabatic compression, which consists of a one-air treatment process, (a) a pre-vacuum process to reduce the air inside the fabric and the steam pot, and (b) a temperature lower than the steam set temperature. It consists of four processes: a steam infiltration process that replaces steam with residual air, (1) a steam supply and cent process that actively circulates steam, and (1) a steam exhaust process.

後述する本発明は、この4工程からなる蒸気処理方法を
基盤としてなされたものであるため、ここで、第3図を
参照しながら各工程について詳しく説明する。
Since the present invention, which will be described later, is based on the steam treatment method consisting of these four steps, each step will now be described in detail with reference to FIG. 3.

(ア):前真空工程 蒸気釜(1)内に布帛巻き層(4)を装填し、蒸気釜(
1)を密閉し、バルブ(7)、 (8)及び(14)を
閉じてバルブ(to)、 (11)及び(13)を開き
、真空ポンプ(16)を駆動して蒸気釜(1)内の空気
を排出し、蒸気釜内圧力を一600mm)(g以下の高
真空圧にする。この操作により布帛巻き層(4)内に含
まれる空気の相当量が排除され巻き層(4)内への蒸気
の流通が容易になる。
(A): Pre-vacuum step The fabric wrapping layer (4) is loaded into the steam pot (1), and the steam pot (
1), close the valves (7), (8) and (14), open the valves (to), (11) and (13), and drive the vacuum pump (16) to release the steam pot (1). The air inside the steam pot is discharged, and the pressure inside the steam pot is brought to a high vacuum pressure of -600 mm) (g or less). Through this operation, a considerable amount of the air contained in the fabric wrapped layer (4) is removed, and the wrapped layer (4) This facilitates the flow of steam into the interior.

(イ):蒸気浸透工程 バルブ(11)を閉してバルブ(8)を開き、京気供給
5(9)より蒸気バイブ(5)の噴出孔(6)を介して
蒸気を蒸気釜(1)内に送入する。この送入された蒸気
は、布帛巻き層(4)を貫いて流通し噴出孔(3)から
シリンダー(2)内に入D、真空ポンプ(16)の作動
によってバルブ(10)及び(13)を経て蒸気釜(1
)外に排出される。蒸気釜(1)内に送入された蒸気は
布帛巻き層(4)を貫いて流通する間に熱交換を行い布
帛を加熱するが、その温度はセット時の所望の処理温度
よりも低くなるように蒸気送入量及び/または排出量を
111節する。即ち、仄気釜内圧力が・所定の圧力上限
値よりも高くなったとき(温度が上昇し過ぎたとき)、
バルブ(8を閉じて蒸気の送入を停止し、真空ポンプ(
16)の排出操作により蒸気釜内圧力を低下させる。ま
た、蒸気釜内圧力が所定の圧力下限値よりも低くな−、
たとき(温度が低下し過ぎたとき)、バノ【を閉じて蒸
気の排出を停止し蒸気釜内圧力を上昇させる。
(B): Close the steam infiltration process valve (11), open the valve (8), and supply steam from the Keiki supply 5 (9) to the steam pot (1 ). The introduced steam passes through the fabric-wound layer (4) and enters the cylinder (2) from the nozzle hole (3), and is then moved through the valves (10) and (13) by the operation of the vacuum pump (16). After passing through the steam kettle (1
) is discharged outside. The steam introduced into the steam pot (1) passes through the fabric wrapping layer (4) and heats the fabric through heat exchange, but the temperature becomes lower than the desired processing temperature at the time of setting. Section 111 shows the amount of steam input and/or discharged. In other words, when the pressure inside the steam oven becomes higher than the predetermined upper pressure limit (when the temperature rises too much),
Close the valve (8) to stop the supply of steam, and turn on the vacuum pump (
16) The pressure inside the steam pot is reduced by the discharging operation. Also, if the pressure inside the steam pot is lower than the predetermined lower limit of pressure,
(when the temperature drops too much), the stove is closed to stop the discharge of steam and increase the pressure inside the steam pot.

そして、この圧力が所定の圧力下限値と圧力上限値との
範囲を外れたとき、再びバルブ(8)あるいは(10)
を開き蒸気を送入または排出する。この操作を所定時間
繰り返すことにより巻き層(4)内の空気は完全に蒸気
によって置換される。このスス漫ろ工程に要−する時間
は、−+aに30秒から180秒間である。
Then, when this pressure is out of the range between the predetermined pressure lower limit value and pressure upper limit value, the valve (8) or (10) is activated again.
open to let steam in or out. By repeating this operation for a predetermined period of time, the air in the wound layer (4) is completely replaced by steam. The time required for this soot smoothing process is 30 seconds to 180 seconds.

(つ):蒸気送入及びセット工程 バルブ(lO)及び(13)を閉じて真空ポンプ(16
)を停止し、バルブ(7)及び(8)を開いて、布帛巻
き層(4)の内外両側から蒸気送入を行う。そして、蒸
気釜(1)内の温度が所定の温度まで上昇したらバルブ
(7)及び(8)を閉じて蒸気送入を停止し、この温度
で所定時間(一般に1分から10分間)処理をm、続す
る。
(1): Close the steam supply and set process valve (lO) and (13), and close the vacuum pump (16).
), valves (7) and (8) are opened, and steam is introduced from both the inside and outside of the fabric-wound layer (4). When the temperature inside the steam pot (1) rises to a predetermined temperature, the valves (7) and (8) are closed to stop the steam supply, and the process is continued at this temperature for a predetermined time (generally 1 to 10 minutes). , continued.

(巧 :蒸気排出工程 バルブ(1,0)、(11)及び(14)を開き、蒸気
釜(1)内の茶気を排出して蒸気釜(1) 内の圧力を
大気圧と等しくした後、巻き層(4)をシリンダー(2
)と共に蒸気釜(1)外に取り出す。
(Takumi: Open the steam discharge process valves (1, 0), (11), and (14) to exhaust the steam inside the steam pot (1) and equalize the pressure inside the steam pot (1) with atmospheric pressure. After that, roll the rolled layer (4) into a cylinder (2
) and take it out of the steam pot (1).

以上の4つの工程からなる布帛の蒸気処理方法は、上述
のように最初の前真空工程において憂い真空能力(時間
3分程度で大気圧より一600mmHg以下に到達)を
必要とし、次の蒸気浸透工程においては布帛内の蒸気流
通時間を長くして十分な熱交換を行うために低い真空能
力を必要とするものである。
The fabric steam treatment method, which consists of the above four steps, requires a high vacuum capacity (reaching 1,600 mmHg or less from atmospheric pressure in about 3 minutes) in the first pre-vacuum step, as mentioned above, and the next step is vapor penetration. The process requires a low vacuum capacity in order to lengthen the steam flow time within the fabric and perform sufficient heat exchange.

従来は、これに対し、能力の異なる真空ポンプを2台設
けたD、あるいは、前真空工程用の高真空圧力、蒸気浸
透工程用の低真空圧力を夫々設定し、1台の真空ポンプ
でバルブの0N−OFF制御を行うことにより対応して
いた。
Conventionally, D was equipped with two vacuum pumps with different capacities, or a high vacuum pressure for the pre-vacuum process and a low vacuum pressure for the steam infiltration process were set, respectively, and a single vacuum pump was used to perform the valve operation. This was handled by performing ON-OFF control.

〔発明が解・決しようとする課題〕[Problem that the invention attempts to solve]

しかしながら、前者の如く1つの処理装置に対して真空
ポンプを2台設けることは、価格面、設置面積等の問題
があD、後者のようにバルブのON−OFFwI?Iを
行うことが一般的であった。
However, installing two vacuum pumps for one processing device as in the former case has problems such as cost and installation space. It was common to do I.

ところが、この方法で蒸気処理を施した布帛について厳
密に寸法安定性、@合、光沢等を調べたところ、必ずし
も完全に均一なセットがなされていないことが判明した
。そこで、本発明者らは、その原因を追及すべく鋭意検
討の結果、セントの不均一は蒸気浸透工程における予熱
温度の不均一に起因するものであるとの知見を得た。
However, when the dimensional stability, alignment, gloss, etc. of the fabrics steam-treated using this method were strictly examined, it was found that completely uniform setting was not always achieved. As a result of intensive studies to find the cause, the present inventors have found that the non-uniformity of the cent is caused by the non-uniformity of the preheating temperature in the steam infiltration step.

このことは、蒸気処理工程における布帛巻き層の温度変
化を示す第4図よD、明らかになる。同図において、3
本の曲線は、夫々に布帛巻き層外表面近辺(t−1)、
巻き層中間部(t−2)、及び巻き層芯部(t−3)の
温度変化を表している。
This becomes clear in Figure 4D, which shows the temperature change of the fabric wrapped layer during the steam treatment process. In the same figure, 3
The book curves are near the outer surface of the fabric wrapping layer (t-1),
It shows the temperature change in the middle part of the wound layer (t-2) and the core part of the wound layer (t-3).

即ち、まず前真空工程(ア)において蒸気釜内減圧操作
を行い、次に蒸気浸透工程(イ)において蒸気の蒸気釜
内への送入、蒸気釜外への排出を繰り返すことによD、
巻き層内部の温度を上昇せしめる。
That is, first, in the pre-vacuum step (A), the pressure inside the steam pot is reduced, and then in the steam permeation step (B), steam is repeatedly introduced into the steam pot and discharged to the outside of the steam pot.
The temperature inside the rolled layer is increased.

そこで、この工程における布帛巻き層内各部の温間上昇
を詳細に検討すると、布帛巻き層外表面近辺(t−1)
の温度がまず急激に上昇して短時間に所定の予熱温度に
到達するが、巻き層中間部(t−2)、巻き層芯部(t
−3)との温度上昇速度が異なるために温度差が生し、
この温度差がセット工程おいてセント性の不均一を引き
起こす原因となっていることが判明した。
Therefore, when we examine in detail the warm rise in each part of the fabric-wrapped layer in this process, we find that near the outer surface of the fabric-wound layer (t-1)
The temperature first rises rapidly and reaches the predetermined preheating temperature in a short time, but the temperature at the middle part of the winding layer (t-2), the core part of the winding layer (t-2), and the core part of the winding layer (t
-3) A temperature difference occurs because the temperature rise rate is different from that of
It has been found that this temperature difference is the cause of non-uniform centrifugation during the setting process.

また、蒸気浸透工程における布帛巻き層各部の温度差を
セント性の不均一を引き起こさない範囲内にするために
、蒸気浸透工程時間を長くするという解決方法があるが
、蒸気処理工程に要する時間が長くなD、生産性がひど
く低下することを免れない。
In addition, in order to keep the temperature difference between each part of the fabric-wound layer during the steam infiltration process within a range that does not cause unevenness of centrifugation, there is a solution of increasing the time of the steam infiltration process, but the time required for the steam treatment process is Long D, productivity will inevitably decline.

本発明は、このような実情に鑑みなされたものであって
、布帛の蒸気処理工程において、1台の真空ポンプにて
所望の蒸気浸透時間で効率的に均一な蒸気処理を施しう
る布帛の蒸気処理方法及びそれに用いる装置の提供を目
的とするものである。
The present invention has been made in view of the above circumstances, and provides a fabric steam treatment process that can efficiently and uniformly steam-treat a fabric with a desired steam penetration time using one vacuum pump in a fabric steam treatment process. The purpose of this invention is to provide a processing method and a device used therefor.

〔課題を解決するための手段〕[Means to solve the problem]

上記の目的は、本発明方法、即ち、密閉蒸気釜内に布帛
巻き層を装填してこれに蒸気処理を施す方法において、 ■蒸気釜と真空ポンプとの間で空気排出用配管を経由せ
しめて蒸気釜内の空気を排出し、蒸気釜内の圧力を高真
空圧にする工程と、 ■蒸気を前記布帛巻き層を貫いて流通させ、この流通し
た蒸気を、蒸気釜と真空ポンプとの間で前記工程[1]
における空気排出用配管の口径より小なる口径の空気排
出用配管を経由せしめて排出することによって、布帛巻
き層内の温度を所望の処理温度より低い温度で保持して
蒸気と残留空気との置換を行う工程と、 ■布帛巻き層の外表部と芯部との両側から茎気送入を行
い、前記所望の処理温度で所定時間セットする工程と、 からなることを要旨とする布帛の蒸気処理方法によって
達成される。
The above object is achieved in the method of the present invention, that is, in the method of loading a fabric wrapped layer into a closed steam pot and subjecting it to steam treatment, A process of discharging the air in the steam pot and increasing the pressure in the steam pot to a high vacuum pressure; (2) passing the steam through the fabric-wrapped layer, and transferring this circulating steam between the steam pot and the vacuum pump; The above step [1]
By discharging the air through an air exhaust pipe with a diameter smaller than that of the air exhaust pipe in the process, the temperature inside the fabric wound layer is maintained at a temperature lower than the desired processing temperature, and steam and residual air are replaced. (1) introducing stem air from both sides of the outer surface and core of the fabric wrapping layer and setting it at the desired treatment temperature for a predetermined period of time. achieved by the method.

そして、上記の方法は、装填された布帛巻き層に蒸気処
理を施す蒸気釜と、この蒸気釜に連結されて蒸気の供給
及び空気の排出を行う2本の配管A、Bと、蒸気供給源
と、前記2本の配管A、  Bから夫々分岐して茶気供
給源に連結される2本の蒸気供給用配管A1、B1及び
夫々の配管AlB1に設けられたバルブと、前記2本の
配管ABから夫々分岐して空気排出部または空気、蒸気
排出用真空ポンプに連結される2本の空気排出用配管A
2.B2及び夫々の配管A2.B2に設けられたバルブ
と、この2本の配管A2.B2から夫々分岐して空気排
出部に連結される空気排出用配管C及びこの配管Cに設
けられたバルブと、同じく前記2本の配管A2.B2か
ら夫々分岐して空気、蒸気排出用真空ポンプに連結され
る2本の空気排出用配管D、E及び夫々の配管D、Eに
設けられたバルブとを設けてなD、且つ前記2本の配管
D、Eにおいて、いずれか一方の配管の口径を他方より
小としたことを要旨とする布帛の茶気処理装置により実
現することができる。
The above method includes a steam pot for steam-treating the loaded fabric wrap layer, two pipes A and B connected to the steam pot for supplying steam and discharging air, and a steam supply source. and two steam supply pipes A1 and B1 which are branched from the two pipes A and B and connected to the brown air supply source, and valves provided on the respective pipes AlB1, and the two pipes Two air exhaust piping A branched from AB and connected to an air exhaust section or a vacuum pump for air and steam exhaust.
2. B2 and each piping A2. The valve installed in B2 and these two pipes A2. Air exhaust piping C branched from B2 and connected to the air exhaust part, and a valve provided on this piping C, and the same two piping A2. Two air exhaust pipes D and E are branched from B2 and connected to a vacuum pump for air and steam exhaust, and valves are provided on the respective pipes D and E, and the two pipes D and E are provided. In the pipes D and E, the diameter of one of the pipes is made smaller than the other.

〔作用〕[Effect]

上記のような構成をとる本発明方法によれば、密閉され
た蒸気釜内に充填された巻き層状の布帛に対し、1台の
真空ポンプにて所望の痕気浸遇時間で効率的に、均一な
蒸気処理を施しうる。即ち、蒸気浸透工程において、前
真空工程よりも小口径の配管を経由せしめて蒸気の排出
を行うことによD、布帛巻き層内に蒸気を充分に流通さ
せることができ、その外表部においても芯部においても
均一な蒸気処理を施すことが可能となるのである。
According to the method of the present invention having the above-described structure, a rolled layered fabric filled in a sealed steam pot can be efficiently soaked with trace air for a desired time using one vacuum pump. Uniform steam treatment can be performed. That is, in the vapor permeation process, by discharging the vapor through a pipe with a smaller diameter than in the pre-vacuum process, it is possible to sufficiently circulate the vapor within the fabric-wrapped layer, and even on the outer surface of the fabric. This makes it possible to perform uniform steam treatment even on the core.

〔実施例〕〔Example〕

以下、本発明の実施例を図面に基づき説明する。 Embodiments of the present invention will be described below based on the drawings.

第1図は本発明装置の一実施例を示し、(1)から(1
1)、(13)から(16)は第3図に基づき説明した
従来方法を実施する装置と同様であD、同一部分もしく
は相当部分に同一符号を記している。よって、これらの
部分の詳細説明は省略する。
FIG. 1 shows an embodiment of the device of the present invention, and shows (1) to (1)
1), (13) to (16) are similar to the apparatus for carrying out the conventional method explained based on FIG. Therefore, detailed explanation of these parts will be omitted.

然して、本発明装置の特徴はその配管系にあD、特に、
蒸気釜(1)と真空ポンプ(16)との間に架設された
配管Eと平行に、配管Eより口径の小なる配管り及びこ
の配管りにおけるバルブ(12)を設けたところにある
。以後、配管りを小口径の配管D、配管Eを大口径の配
管Eと呼ぶ。
However, the feature of the device of the present invention is its piping system, especially:
Parallel to the pipe E installed between the steam pot (1) and the vacuum pump (16), a pipe with a diameter smaller than that of the pipe E and a valve (12) in this pipe are provided. Hereinafter, the piping will be referred to as small-diameter piping D, and the piping E will be referred to as large-diameter piping E.

この小口径の配管りと大口径の配管Eとの口径比率は、
両配管D、E内の流体の流量比率を決定するものである
The diameter ratio of this small diameter piping and large diameter piping E is:
This determines the flow rate ratio of fluids in both pipes D and E.

そこで、口径比率と流量比率の関係を求めるため、流体
力学におけるBernoulli の定理、連続の式を
もとに、単位長さあたりの損失ヘッドはすべて管路損失
(管摩擦損失+バルブにおけるtM失)管FJ擦係数は
Blasiusの実験式、バルブにおける)置去係数は
口径によらず一定であるとして、下記の式をたて、計算
を行った。
Therefore, in order to find the relationship between the diameter ratio and the flow rate ratio, based on Bernoulli's theorem and continuity equation in fluid mechanics, the head loss per unit length is the pipe loss (pipe friction loss + tM loss in the valve). The pipe FJ friction coefficient was calculated using Blasius's experimental formula, and the displacement coefficient (in the valve) was assumed to be constant regardless of the diameter, and the following formula was established for calculation.

<Bernoulli の定理〉 小口径側: V+in”/2g+P1in/  T +
Z1in=V out”/2g + P+out/ r
 + Z+out + hl■大口径側: Vain”
/2g + Pzin/ T + Zzin = V、
out2/2g + Pgout/ r + Z2ou
t + h2■く連続の弐〉 小口径側:V、in^、in = V、outA+ou
L■大口径側: VtinAgin−ν2outAzo
ut■ただし、V:流速    P:圧力 Z:位Iヘッド d:口径 A:断面積   h:損失へ、ド g:重力加速度 γ:比重量 添字は、ln:入口側  out :出口側1:小口径
側  2;大口径側 を表す。
<Bernoulli's theorem> Small diameter side: V+in"/2g+P1in/T +
Z1in=V out”/2g + P+out/r
+ Z + out + hl ■Large diameter side: Vain”
/2g + Pzin/ T + Zzin = V,
out2/2g + Pgout/r + Z2ou
t + h2■ Continuous 2> Small diameter side: V, in^, in = V, outA+ou
L■Large diameter side: VtinAgin-ν2outAzo
ut■ However, V: flow velocity P: pressure Z: position I head d: diameter A: cross-sectional area h: to loss, deg: gravitational acceleration γ: specific weight subscript is ln: inlet side out: outlet side 1: small Diameter side 2: represents the large diameter side.

まず、入口側と出口側とで夫々の口径は等しいので ■弐においてAl1n = AboutよりV、1n=
V1ouL =V■弐においてL in = Lout
 よりt++=P+in/  γP+out/ T ■弐においてLin = ZzoutよりJ−7in/
rPzout/ γ 夫々の配管において入口側と出口側との圧力差は等しい
ので、hI=hzが導ける。 tX失ヘッドは、h −
(λml/d + 0*V”/2g  (λ:管摩擦頃
失係数ζ;バルブ損失係数 1:管路長さ)で表され、
h+=hzより次式が成立する。
First, since the diameters of the inlet and outlet sides are the same, on the second side, Al1n = About, V, 1n =
V1ouL = V■2, L in = Lout
From t++=P+in/ γP+out/ T ■At the second Lin = J-7in/ from Zzout
rPzout/ γ Since the pressure difference between the inlet side and the outlet side of each pipe is equal, hI=hz can be derived. tX lost head is h −
It is expressed as (λml/d + 0*V”/2g (λ: pipe friction lapse coefficient ζ; valve loss coefficient 1: pipe length),
Since h+=hz, the following equation holds true.

(λ +本し/d+  +  c+)*v+”/2g 
 −(λ t”lt/d@  +ζ 2)本Vg”/2
g  ■ この0式よD、vlとv2との関係を計算した。その結
果を表に示す。
(λ + book/d+ + c+)*v+”/2g
−(λ t”lt/d@ +ζ 2) Book Vg”/2
g ■ Using this formula 0, we calculated the relationship between D, vl, and v2. The results are shown in the table.

上表よD、口径比率と流量比率との関係が明らかになる
。通常、真空ポンプへの配管口径は真空ポンプ吸い込み
口径と同一とし、小口径の配管で絞って流量を下げるこ
とは実施しないが、本発明においては逆に、求めた表に
基づき真空ポンプの吸い込み口径に比べて配管口径を小
とすることによD、吸い込み量を減少させる。
In the table above, the relationship between the diameter ratio and the flow rate ratio becomes clear. Normally, the diameter of the piping to the vacuum pump is the same as the suction diameter of the vacuum pump, and the flow rate is not reduced by throttling the piping with a small diameter.However, in the present invention, on the contrary, the suction diameter of the vacuum pump is determined based on the table obtained. By making the pipe diameter smaller than D, the amount of suction is reduced.

本発明における効果、即ち前真空工程と蒸気浸透工程と
において真空能力に差をつけるためには、大口径3イン
チに対して小口径は2172インチ以下とするが、これ
を極端に小口径とすると、3インチに対して172イン
チで流量比率が100;1.2というように閉塞状態と
なってしまうため、1/2インチ以上に設定することと
する。
In order to achieve the effect of the present invention, that is, to differentiate the vacuum capacity between the pre-vacuum process and the steam infiltration process, the small diameter is set to 2172 inches or less compared to the large diameter of 3 inches, but if this is made extremely small, , the flow rate ratio is 100:1.2 at 172 inches compared to 3 inches, resulting in a blocked state, so it is set to 1/2 inch or more.

第2図は、本実施例の装置を用いて布帛の蒸気処理を行
ったときの布帛巻き層外表面ma(t−1)1巻き層中
間部(t−2)、及び巻き層芯部(t−3>の温度変化
を表している。蒸気浸透工程(イ)における布帛巻き層
内各部の温度上昇を詳細に検討すると、布帛巻き層外表
面近辺(t−1)の温度がまず急激に上昇する。この際
、巻き層中間部(t−2)、巻き層芯部(t−3)との
温度上昇速度が異なるが、茶気排出速度が遅いため、布
帛巻き層通過時間が長く熱交換が十分に行われ、布帛各
部の温度上昇の差が少なくなる。また、短時間での蒸気
浸透が可能となる。
FIG. 2 shows the outer surface ma (t-1) of the fabric wound layer, the middle part (t-2) of the first wound layer, and the core part (t-2) of the wound layer when the fabric was steam-treated using the apparatus of this example. t-3>.A detailed study of the temperature rise in each part of the fabric-wrapped layer in the vapor infiltration process (a) reveals that the temperature near the outer surface of the fabric-wound layer (t-1) first rapidly increases. At this time, the rate of temperature increase is different between the middle part of the wound layer (t-2) and the core part of the wound layer (t-3), but because the brown air discharge rate is slow, the time for the fabric to pass through the wound layer is long, and the temperature rises. The exchange is carried out sufficiently, and the difference in temperature rise between each part of the fabric is reduced. Also, vapor penetration becomes possible in a short time.

このように、蒸気浸透工程(イ)の間に布帛各部を経て
蒸気処理を完了する。
In this way, the steam treatment is completed through each part of the fabric during the steam infiltration step (a).

〔具体例〕〔Concrete example〕

上述の本実施例の装置に、小口径の配管として2インチ
管、大口径の配管として3インチ管(真空ポンプ吸い込
み側口径)を用いた。このときの流量比率は、約4:1
0である。
In the apparatus of this example described above, a 2-inch pipe was used as the small-diameter pipe, and a 3-inch pipe (diameter on the suction side of the vacuum pump) was used as the large-diameter pipe. The flow rate ratio at this time is approximately 4:1
It is 0.

この装置を用いて、純毛織物及び合!1lIi混毛織物
の処理を以下のように実施した。
Using this device, you can create pure wool fabrics and fabrics! The treatment of the 1lIi mixed wool fabric was carried out as follows.

(ア):前真空工程 蒸気釜(1)内に布帛巻き層(4)を装填して蒸気釜(
1)を密閉し、(7)、 (8)及び(14)を閉じて
バルブ(10) 、 (11)及び(13)、あるいは
バルブ(10)、(11)、(13)及び(12)を開
き、真空ポンプ(16)を駆動して蒸気釜(1)内の空
気を排出し、蒸気釜内圧力を600mmHg以下の高真
空圧にする。この圧力については、被処理布帛の種類等
によって適宜設定されうるが、−700mmHg以下と
することによD、巻き層内への蒸気の流通が一暦スムー
ズになり好適である。
(A): Pre-vacuum step The fabric wrapping layer (4) is loaded into the steam pot (1) and the steam pot (
1) and close (7), (8) and (14) to open valves (10), (11) and (13), or valves (10), (11), (13) and (12). is opened, the vacuum pump (16) is driven to exhaust the air inside the steam pot (1), and the internal pressure of the steam pot is brought to a high vacuum pressure of 600 mmHg or less. This pressure can be set as appropriate depending on the type of fabric to be treated, etc., but it is preferable to set it to -700 mmHg or less, as D, the steam can flow smoothly into the wound layer over a period of time.

(イ):蒸気浸透工程 バルブ(11)及び(13)を閉じてバルブ(8) を
開き、蒸気供給源(9)より蒸気パイプ(5)の噴出孔
(6)を介して蒸気を蒸気釜(1)内に送入する。この
送入された蒸気は布帛巻き層(4)を貫いて流通し、噴
出孔(3)からシリンダー(2)内に入D、真空ポンプ
(16)の作動によってバルブ(10)及び小口径の配
管りに設けられたバルブ(12)を経て蒸気釜(1)外
に排出される。このとき、蒸気釜(1)内に送入された
蒸気は布帛巻き層(4)を貫いて流jIiする間に布帛
を加熱するが、その温度は所望のセット時の処理温度よ
りも低(なるように蒸気送入量及び/または排出量をバ
ルブ(8)あるいは(12)を開くことにより調節する
。小口径のバイパス配管りに設けられているバルブ(1
2)は、釜内圧力が所定の圧力上限値を越えたときの蒸
気排出時の排出速度を低下させる。これによD、布帛巻
き層(4)内を1気が流通する時間の不足がなくなる。
(b): Steam infiltration process Close the valves (11) and (13), open the valve (8), and supply steam from the steam supply source (9) to the steam pot through the jet hole (6) of the steam pipe (5). (1) Send within. This introduced steam passes through the fabric-wrapped layer (4), enters the cylinder (2) from the nozzle hole (3), and is driven by the valve (10) and small-diameter cylinder (D) through the operation of the vacuum pump (16). It is discharged to the outside of the steam pot (1) through a valve (12) provided in the piping. At this time, the steam introduced into the steam pot (1) passes through the fabric wrapping layer (4) and heats the fabric while flowing, but the temperature is lower than the processing temperature at the desired setting ( The amount of steam fed and/or the amount of steam discharged is adjusted by opening valve (8) or (12).
2) reduces the discharge speed when steam is discharged when the pressure inside the pot exceeds a predetermined pressure upper limit value. This eliminates the shortage of time for the air to flow through the fabric-wound layer (4).

(つ)::i気送入及びセント工程 バルブ(10)及び(12)を閉じて真空ポンプ(16
)を停止しバルブ(7)及び(8)を開き、布帛巻き層
(4)の内外両側から蒸気送入を行う。
(1)::i Close the air supply and cent process valves (10) and (12) and vacuum pump (16).
), valves (7) and (8) are opened, and steam is introduced from both the inside and outside of the fabric-wound layer (4).

そして蒸気釜(1)内の温度が所定の温度に上昇したな
らばバルブ(7)及び(8)を閉して茶気送入を停止し
、この温度で所定時間(一般に1分から10分間)処理
を継続する。
When the temperature inside the steam pot (1) rises to a predetermined temperature, valves (7) and (8) are closed to stop the supply of tea air, and the temperature is maintained at this temperature for a predetermined period of time (generally 1 to 10 minutes). Continue processing.

(I):蒸気排出工程 バルブ(10)、(11)及び(14)を開き蒸気釜(
1)内の蒸気を排出し蒸気釜(1)内の圧力を大気圧と
等しくした後、巻き層(4)をシリンダー(2)と共に
蒸気釜(1)外に取り出す。
(I): Open the steam discharge process valves (10), (11) and (14) and the steam pot (
1) After discharging the steam inside the steam pot (1) and making the pressure inside the steam pot (1) equal to atmospheric pressure, the wound layer (4) is taken out of the steam pot (1) together with the cylinder (2).

以上のように処理を行うと、第2図に基づき前述した如
く蒸気浸透工程において巻き層中間部(t−2)及び巻
き層芯部(t−3)についても均一に温度が上昇し、温
度差によるセント性の不拘−p問題が解消されることと
なD、その結果、この処理を施した純毛織物1合繊混毛
織物がともに寸法安定性及び風合に優れ、且つ美しい光
沢を有するものとなることが61 iEされた。
When the above-mentioned treatment is carried out, as described above based on FIG. The problem of inconsistency in centility due to the difference is resolved.As a result, both the pure wool fabric and synthetic fiber blend fabric subjected to this treatment have excellent dimensional stability and texture, and have a beautiful luster. It became 61 iE.

〔発明の効果〕〔Effect of the invention〕

以上述べた通D、本発明方法によれば、布帛の蒸気処理
工程において、1台の真空ポンプのみを用い、所望の蒸
気浸透時間にて均一な蒸気セットを施すことが可能十な
る。
As stated above, according to the method of the present invention, in the fabric steam treatment process, it is possible to uniformly set the steam at a desired steam penetration time using only one vacuum pump.

また、本発明装置は、従来方法に用いていた装置に対し
特に複雑な機構を設けることを必要とせず1、設備コス
トも安価で、確実に本発明の蒸気処理方法を実現しうる
ちのである。
Furthermore, the apparatus of the present invention does not require any particularly complicated mechanism compared to the apparatus used in the conventional method1, and the equipment cost is low, making it possible to reliably realize the steam treatment method of the present invention. .

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

第1図は本発明装置の一実施例を示す概略説明図、第2
図は本発明方法における布帛巻き層各部の温度変化を示
す図、第3図は従来の蒸気処理方法を実施する装置の一
例を示す概略説明図、第4図は従来方法における布帛巻
き層各部の温度変化を示す図である。 (1)・・・蒸気釜      (2)・・・シリンダ
ー(4)・・・布帛巻き層    (5)・・・蒸気パ
イプ(12)・・・小口径配管におけるバルブ(16)
・・・真空ポンプ
FIG. 1 is a schematic explanatory diagram showing one embodiment of the device of the present invention, and FIG.
The figure shows the temperature changes in each part of the fabric-wound layer in the method of the present invention, Fig. 3 is a schematic explanatory diagram showing an example of an apparatus for carrying out the conventional steam treatment method, and Fig. 4 shows the temperature changes in each part of the fabric-wound layer in the conventional method. FIG. 3 is a diagram showing temperature changes. (1)...Steam pot (2)...Cylinder (4)...Fabric wrapping layer (5)...Steam pipe (12)...Valve in small diameter piping (16)
···Vacuum pump

Claims (2)

【特許請求の範囲】[Claims] (1)密閉蒸気釜内に布帛巻き層を装填してこれに蒸気
処理を施す方法において、 [1]蒸気釜と真空ポンプとの間で空気排出用配管を経
由せしめて蒸気釜内の空気を排出し、蒸気釜内の圧力を
高真空圧にする工程と、 [2]蒸気を前記布帛巻き層を貫いて流通させ、この流
通した蒸気を、蒸気釜と真空ポンプとの間で前記工程[
1]における空気排出用配管の口径より小なる口径の空
気排出用配管を経由せしめて排出することによって、布
帛巻き層内の温度を所望の処理温度より低い温度で保持
して蒸気と残留空気との置換を行う工程と、[3]布帛
巻き層の外表部と芯部との両側から蒸気送入を行い、前
記所望の処理温度で所定時間セットする工程と、 からなることを特徴とする布帛の蒸気処理方法。
(1) In a method of loading a fabric wrapped layer into a closed steam pot and subjecting it to steam treatment, [1] Air in the steam pot is passed through an air exhaust pipe between the steam pot and a vacuum pump to drain the air inside the steam pot. [2] The steam is passed through the fabric-wound layer, and the circulated steam is transferred between the steam pot and the vacuum pump in the step [2].
By discharging the air through an air discharge pipe having a diameter smaller than that of the air discharge pipe in step 1], the temperature within the fabric-wrapped layer is maintained at a temperature lower than the desired processing temperature, and steam and residual air are removed. and [3] introducing steam from both sides of the outer surface and core of the fabric-wound layer and setting it at the desired treatment temperature for a predetermined time. steam treatment method.
(2)装填された布帛巻き層(4)に蒸気処理を施す蒸
気釜(1)と、この蒸気釜(1)に連結されて蒸気の供
給及び空気の排出を行う2本の配管A、Bと、蒸気供給
源(9)と、前記2本の配管A、Bから夫々分岐して蒸
気供給源(9)に連結される2本の蒸気供給用配管A1
、 B1及び夫々の配管A1、B1に設けられたバルブ(7
)、(8)と、前記2本の配管A、Bから夫々分岐して
空気排出部(15)または空気、蒸気排出用真空ポンプ
(16)に連結される2本の空気排出用配管A2、B2
及び夫々の配管A2、B2に設けられたバルブ(10)
、(11)と、この2本の配管A2、B2から夫々分岐
して空気排出部(15)に連結される空気排出用配管C
及びこの配管Cに設けられたバルブ(14)と、同じく
前記2本の配管A2、B2から夫々分岐して空気、蒸気
排出用真空ポンプ(16)に連結される2本の空気排出
用配管D、E及び夫々の配管D、Eに設けられたバルブ
(12)、(13)とを設けてなり、且つ前記2本の配
管D、Eにおいて、いずれか一方の配管の口径を他方よ
り小としたことを特徴とする布帛の蒸気処理装置。
(2) A steam pot (1) that applies steam treatment to the loaded fabric wrap layer (4), and two pipes A and B that are connected to this steam pot (1) and supply steam and discharge air. , a steam supply source (9), and two steam supply pipes A1 branched from the two pipes A and B, respectively, and connected to the steam supply source (9).
, B1 and the valves (7
), (8), and two air exhaust pipes A2 branched from the two pipes A and B, respectively, and connected to an air exhaust part (15) or a vacuum pump (16) for air and steam exhaust; B2
and a valve (10) provided in each pipe A2, B2
, (11), and air exhaust pipes C branched from these two pipes A2 and B2 and connected to the air exhaust part (15).
A valve (14) provided on this pipe C, and two air exhaust pipes D branched from the two pipes A2 and B2 and connected to a vacuum pump (16) for air and steam exhaust. , E and valves (12) and (13) provided in the respective pipes D and E, and in the two pipes D and E, the diameter of one of the pipes is smaller than the other. A fabric steam treatment device characterized by:
JP14015789A 1989-05-31 1989-05-31 Method and device for treating cloth with steam Granted JPH038863A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14015789A JPH038863A (en) 1989-05-31 1989-05-31 Method and device for treating cloth with steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14015789A JPH038863A (en) 1989-05-31 1989-05-31 Method and device for treating cloth with steam

Publications (2)

Publication Number Publication Date
JPH038863A true JPH038863A (en) 1991-01-16
JPH059538B2 JPH059538B2 (en) 1993-02-05

Family

ID=15262194

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14015789A Granted JPH038863A (en) 1989-05-31 1989-05-31 Method and device for treating cloth with steam

Country Status (1)

Country Link
JP (1) JPH038863A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06140578A (en) * 1992-10-29 1994-05-20 Mitsubishi Electric Corp Semiconductor integrated device
JPH0841777A (en) * 1994-07-25 1996-02-13 Kishimoto Kosakusho:Kk High-pressure steamer
JP2005060875A (en) * 2003-08-11 2005-03-10 Nitto Boseki Co Ltd Deoiling apparatus for glass fiber fabric
JP2007265769A (en) * 2006-03-28 2007-10-11 Denso Corp Lid of battery case
CN108457026A (en) * 2018-03-09 2018-08-28 韦贞勇 A kind of textile technology steaming machine

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06140578A (en) * 1992-10-29 1994-05-20 Mitsubishi Electric Corp Semiconductor integrated device
JPH0841777A (en) * 1994-07-25 1996-02-13 Kishimoto Kosakusho:Kk High-pressure steamer
JP2005060875A (en) * 2003-08-11 2005-03-10 Nitto Boseki Co Ltd Deoiling apparatus for glass fiber fabric
JP2007265769A (en) * 2006-03-28 2007-10-11 Denso Corp Lid of battery case
CN108457026A (en) * 2018-03-09 2018-08-28 韦贞勇 A kind of textile technology steaming machine

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