JPS6030388B2 - Processing method and device for textile products - Google Patents
Processing method and device for textile productsInfo
- Publication number
- JPS6030388B2 JPS6030388B2 JP17755981A JP17755981A JPS6030388B2 JP S6030388 B2 JPS6030388 B2 JP S6030388B2 JP 17755981 A JP17755981 A JP 17755981A JP 17755981 A JP17755981 A JP 17755981A JP S6030388 B2 JPS6030388 B2 JP S6030388B2
- Authority
- JP
- Japan
- Prior art keywords
- fabric
- processing
- circulation
- circulation time
- temperature
- 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
Links
- 239000004753 textile Substances 0.000 title claims description 11
- 238000003672 processing method Methods 0.000 title 1
- 239000004744 fabric Substances 0.000 claims description 59
- 238000012545 processing Methods 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 22
- 238000012546 transfer Methods 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 14
- 238000002347 injection Methods 0.000 claims description 13
- 239000007924 injection Substances 0.000 claims description 13
- 239000000975 dye Substances 0.000 claims description 12
- 230000014759 maintenance of location Effects 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 8
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 230000007423 decrease Effects 0.000 claims description 5
- 238000005259 measurement Methods 0.000 claims 1
- 238000004043 dyeing Methods 0.000 description 26
- 238000011282 treatment Methods 0.000 description 7
- 239000000835 fiber Substances 0.000 description 6
- 238000004364 calculation method Methods 0.000 description 5
- 229920000728 polyester Polymers 0.000 description 5
- 238000004061 bleaching Methods 0.000 description 4
- 238000009991 scouring Methods 0.000 description 4
- 239000000986 disperse dye Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 2
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004836 empirical method Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Landscapes
- Treatment Of Fiber Materials (AREA)
Description
【発明の詳細な説明】
この発明は、繊維製品、すなわち彼処理布常を濠端状に
て、循環回動させて、染色・精練・漂白等の処理を行な
う装置における処理温度の制御方法及び装置に関するも
ので、その目的とするところは、布富等の染色・精練・
漂白等の処理、特に染色において、従来の処理時間のい
わゆる不必要な時間を省き、染色工程の合理化を計ろう
とするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling processing temperature in an apparatus for dyeing, scouring, bleaching, etc., by circulating textile products, i.e. processed fabrics, in a moat-like manner, and It is related to equipment, and its purpose is to dye, scouring, and
The aim is to streamline the dyeing process by eliminating so-called unnecessary conventional processing time in treatments such as bleaching, especially in dyeing.
従釆、染色プログラムの決定は、熟練染色技術者が、染
色諸条件を全て経験的に決めていたのがほとんどであっ
た。In most cases, dyeing programs were determined by experienced dyeing engineers who determined all dyeing conditions empirically.
又、その条件の装置への設定方法にしても、たとえば、
温度制御曲線にしても、バッチごとの品種、組織、処理
量、色相等の変化に対して、毎回プログラムを作ること
は日常困難であるので、最大公約数的に、あらかじめ数
種類のパターンを決め、その中から選択し、繰返し使っ
ているので、最適な温度制御は得られず、トラブル発生
を防ぐため、安全率を大きくとるので、どうしても、不
必要な時間が生じて生産性が低下する弊害があった。又
、たまたま、最適な温度曲線が得られたとしても、染色
加工中、布毎の循環速度が変化することがあるが、その
変化が大きい場合、例えば染色条件が、被処理布常速度
300仇/分(循環時間6現砂)にて温度設定してある
のに、布帯速度が240机/分(75秒)まで低下した
とすると、従釆の温度制御方法であると、布常循環の異
常が生じても、無関係に初期設定された通り、温度制御
は進行してしまうので、その結果、染めむら、色違い等
の染色トラブルが生じる欠点があった。更に又、布角速
度が増大(循環時間は短縮)した場合は、染色トラブル
は生じないが、余分な時間をかけることになり不具合で
あった。以上のような布常速度が変化した場合、オペレ
ーターが布岳速度又は温度変化率を修正することは困難
である。Also, regarding the method of setting the conditions on the device, for example,
Even when it comes to temperature control curves, it is difficult to create a program every time to account for changes in variety, texture, processing amount, hue, etc. for each batch, so we decided on several types of patterns in advance based on the greatest common divisor. Since we select from among them and use them repeatedly, we cannot obtain optimal temperature control, and in order to prevent trouble from occurring, we take a large safety factor, which inevitably leads to unnecessary time and reduced productivity. there were. Furthermore, even if the optimum temperature curve is obtained by chance, the circulation speed for each fabric may change during the dyeing process.If the change is large, for example, if the dyeing conditions are such that the normal speed of the processed fabric is 300mm, /min (circulation time: 6 current sand), but if the fabric stripping speed drops to 240/min (75 seconds), if the temperature control method is a secondary one, the fabric is constantly circulating. Even if an abnormality occurs, the temperature control proceeds as initially set regardless, which has the drawback of causing dyeing problems such as uneven dyeing and different colors. Furthermore, if the angular velocity of the cloth is increased (the circulation time is shortened), dyeing problems will not occur, but extra time will be required, which is a problem. When the normal speed of the cloth changes as described above, it is difficult for the operator to modify the cloth speed or the rate of temperature change.
本発明では、温度プログラムの決定を、経験的に決める
のではなく、処理される、品質、組織、処理量及び染料
の種類、処理液量、布速度等の条件設定要因と、染色処
理装置の持つ均染能力とを組み合わせた理想的な染色計
算式を与え、布畠の循環時間を変数として、自動的に演
算修正制御し、上述のような、染色工程の不必要な時間
を省き、人間では困難な操作を全て合理的に制御し、染
色トラブルを防ぎ、高効率の結果を得るようにしたもの
である。即ち、第1の発明は繊維製品(布常)を無端状
で循環回動させて処理する方法において、布常の1循環
時間を検知し、あらかじめ設定された処理条件に基づき
決められた温度プログラムを、布常の1循環時間が増加
(布速度の低下)した時には温度変化率を低減させ、そ
の反対の時には逆となる様に変化に応じ、自動的に布用
の1循環ごとに温度プログラムを修正することを特徴と
する繊維の処理方法にあり、第2の発明は布帯の1循環
ごとに染料や薬品の注入速度も変化させるようにし、更
に最大許容循環時間を設定し、布局の1循環が増大し、
設定最大許容循環時間に達したとき前記染料、薬品の注
入等を一時停止させ、布帯の循環が再び許容循環時間内
に戻ったのを確認し、再度制御を開始することを特徴と
する繊維製品の処理方法にあり、第3の発明は上記第1
の発明を実施する菱贋。すなわち、移送管と、滞溜槽と
、これら移送管及び滞溜槽で形成される環状の処理通路
と、該通路中に設けられた上記移送管の上流機に対する
被処理布尾の送り込み手段と、上記滞溜槽底部より循環
ポンプを介して移送管の上流端部に開口された噴射ノズ
ルに通ずる処理液循環通路と、該通路途中に介在された
処理液の温度調節装置と、上記環状の処理通路を移送さ
れる被処理布常に付設した被測定体と、これに対応する
少なくとも1ケ以上の検知体を設けたことを特徴とする
繊維製品の処理装置にある。次にこの発明を図面に示す
実施例に基づいて説明する。第1図において、1は瀞溜
槽で、これと移送管2で環状処理通路を形成している。In the present invention, the temperature program is not determined empirically, but is determined based on condition setting factors such as the quality, structure, processing amount, type of dye, processing liquid amount, cloth speed, etc., and the dye processing equipment. We provide an ideal dyeing calculation formula that combines the level dyeing ability of the company, and automatically control calculation correction using the cloth circulation time as a variable, eliminating unnecessary time in the dyeing process as described above, In this method, all difficult operations are rationally controlled, dyeing troubles are prevented, and highly efficient results are obtained. That is, the first invention is a method of processing textile products by circulating them in an endless manner, in which one circulation time of the textile is detected and a temperature program is determined based on preset processing conditions. , the temperature change rate is reduced when the cloth circulation time increases (fabric speed decreases), and vice versa, and the temperature is automatically programmed for each cloth circulation. The second invention is a method for processing fibers, which is characterized by changing the injection rate of dyes and chemicals for each circulation of the fabric strip, further setting the maximum allowable circulation time, and adjusting the amount of fabric. 1 circulation increases,
A textile characterized in that when a set maximum allowable circulation time is reached, the injection of the dye or chemical is temporarily stopped, and after confirming that the circulation of the cloth band has returned to within the allowable circulation time, the control is restarted. The third invention resides in a method for treating a product, and the third invention is the first invention described above.
Ryokan implementing the invention of. That is, a transfer pipe, a retention tank, an annular processing passage formed by the transfer pipe and the retention tank, a means for feeding the tail of the treated fabric to an upstream machine of the transfer pipe provided in the passage, and A processing liquid circulation passage leading from the bottom of the retention tank via a circulation pump to an injection nozzle opened at the upstream end of the transfer pipe, a temperature control device for the processing liquid interposed in the middle of the passage, and the annular processing passage. A textile processing apparatus is provided, characterized in that a measuring object is always attached to the processed cloth to be transferred, and at least one or more sensing objects corresponding thereto are provided. Next, the present invention will be explained based on embodiments shown in the drawings. In FIG. 1, reference numeral 1 denotes a sump tank, and this and a transfer pipe 2 form an annular processing passage.
3は被処理布常の出入口で開閉自在に構成されている。Reference numeral 3 is an entrance/exit for the cloth to be treated, and is configured to be openable and closable.
4は滞溜槽1に閉口する液吸込口、5は該吸込口とポン
プ6の吸引側を蓮通する吸込配管、7はポンプ6の吐出
側と移送管2の上流端部とを蓮通する吐出配管で、配管
途中にフィルター8、熱交換器9が設けられている。1
9は熱媒体入口、201ま熱媒体出口を示す。4 is a liquid suction port that closes to the retention tank 1; 5 is a suction pipe that connects the suction port with the suction side of the pump 6; and 7 is a suction pipe that connects the discharge side of the pump 6 with the upstream end of the transfer pipe 2. A filter 8 and a heat exchanger 9 are provided in the discharge piping. 1
9 indicates a heat medium inlet, and 201 indicates a heat medium outlet.
吸込04から吸込まれた液は吸込配管5、ポンプ6、吐
出配管7、フィルター8、熱交換器9、処理液噴射部1
0を経て、移送管2の上流端部から総溜槽1へ戻るよう
になっている。11は被処理布帯の移送管への送り込み
を行なう変速モーター付、又は変速装置付リール又はロ
ールで駆動装置を示す。The liquid sucked from the suction 04 is transferred to a suction pipe 5, a pump 6, a discharge pipe 7, a filter 8, a heat exchanger 9, and a processing liquid injection unit 1.
0, and returns to the general storage tank 1 from the upstream end of the transfer pipe 2. Reference numeral 11 denotes a drive device with a variable speed motor or a reel or roll with a variable speed device for feeding the fabric to be treated into the transfer pipe.
12は被処理布常、13は処理液面、14は処理液噴射
調節弁、15は検出器、16は布常に取付けられた被測
定体、17は移送管の下流端と滞溜槽の一端をつなぐ蓮
通部、18は気相部を示す。12 is the cloth to be treated, 13 is the treatment liquid level, 14 is the treatment liquid injection control valve, 15 is the detector, 16 is the object to be measured attached to the cloth, and 17 is the downstream end of the transfer pipe and one end of the retention tank. The lotus passage section 18 indicates a gas phase section.
この実施例においては、被処理布富12は、布送り込み
リール又はロール11により液面より引上げられ、処理
液噴射部10を経て移送管2内を移行し、他端連通部1
7より沼溜槽1へ導入される。In this embodiment, the fabric to be treated 12 is pulled up from the liquid level by the fabric feeding reel or roll 11, passes through the processing liquid injection part 10, moves inside the transfer pipe 2, and is transferred to the communication part 1 at the other end.
7, it is introduced into the swamp tank 1.
布帯は滞溜槽1内を速度を減じながら前方へ移動し、再
び布送り込みリール又は、ロール11により引上げられ
て、処理液噴射部10により移送管2へ移行される。こ
のように環状処理通路を循環する間に被処理布尾は染色
、精練、漂白、リラックス等の処理が行なわれる。今、
第1図の装置にて、ポリエステル100%の布常を分散
染料を用いて染色加工する場合を例として制御方法を説
明する。The fabric strip moves forward in the retention tank 1 while decreasing its speed, is pulled up again by the fabric feed reel or roll 11, and transferred to the transfer pipe 2 by the treatment liquid spraying section 10. While circulating through the annular processing path in this manner, the treated fabric tail is subjected to treatments such as dyeing, scouring, bleaching, and relaxing. now,
The control method will be explained by taking as an example the case where a 100% polyester cloth is dyed using a disperse dye using the apparatus shown in FIG.
被処理布富12が環状処理通路を循環することにより、
被処理布常12に取付けられた被測定体16が、瀞溜槽
1に取付けられた検出器15を通過するたびに、1循環
時間t(秒)を測定することができる。By circulating the treated cloth wealth 12 through the annular treatment passage,
Each time the object to be measured 16 attached to the treated cloth 12 passes through the detector 15 attached to the sump tank 1, one circulation time t (seconds) can be measured.
分散染料によるポリエステル繊維の染色は一般的に次の
風式にて温度上昇率を決めることができるので被測定体
16が検出器15を通過するために、その測定値t(秒
)を図示されてない演算器に入れて、下記■,胸′式に
よりTを算出し図示されてない温度調節装置に指令を出
し、熱媒体入口19と熱媒体出口20部分にて処理液の
温度制御を行なう。When dyeing polyester fibers with disperse dyes, the rate of temperature rise can generally be determined using the following equation. The temperature of the processing liquid is controlled at the heat medium inlet 19 and the heat medium outlet 20 by calculating T using the following equation (1) and issuing a command to a temperature control device (not shown). .
T=等隻豊 ・‐‐‐‐・風
vf=総 ・・.・・・風
T・・・・・・温度変化率(℃/分)
V・・・・・・染料の最大吸収速度(%/℃・分)L・
・・・・・布の全長(L)Vf・・・・・・布速度(m
/分)
Kf・・・・・・染色装置の均梁能力(%/サイクル)
第2図は一般的なポリエステル繊維の染色温度曲線を示
したものである。T=Tofutsu ・---・Wind vf=Total... ...Wind T...Temperature change rate (℃/min) V...Maximum absorption rate of dye (%/℃・min) L・
...Full length of fabric (L) Vf...Fabric speed (m
/min) Kf... Evening beam capacity of dyeing equipment (%/cycle)
FIG. 2 shows the dyeing temperature curve of common polyester fibers.
第3図は、第2図のT2一T3温度間の布常1循環ごと
の温度上昇率を説明したものである。FIG. 3 illustrates the temperature increase rate for each cycle of the fabric between the temperatures T2 and T3 in FIG. 2.
第3図において、a点までは、ほとんど布常の循環時間
がt=60秒であったのが、何んらかの原因で、tの値
が変化し始めた。そうするとb点からc点に示す間の温
度上昇率は、a点からb点の循環時間t=6の砂を■式
にて計算して得たデータを温度調節装置に指令を出し制
御される。次にb点からc点の循環時間はt=69砂で
あるので、c点で検出器15が検知した時点で、今度は
、b点からc点の循環時間t=69吻こて計算したデー
タでc点よりd点まで温度調節装置が働くことになる。
このような動作を繰返すが、許容循環時間(オーバータ
イム)t′を設定しておくと、例えば第3図の場合r=
7の砂であるので、設定時間t′を超えた時点から温度
調節装置の制御を停止させ、次の検出器15が検知指令
を出すまで待機する。以上、演算式を用いて布常の1循
環時間を変数として温度変イb率を制御する以外に、別
の方法として過去の経験に基づき決めた温度プログラム
を、単純に、布常の1循環時間の増減の割合により温度
変イG率を変化させ、たとえば布帯の1循環時間が1%
増加(布速低下)した時変イB率を1%低下させるなど
の方法もできる。又、以上のように、自動的に布帯の1
循環ごとに温度プログラムを設定する方法において、何
らかの要因で、その温度設定値に追従しないなど測定値
と設定値の偏差が大きくなるとプログラムを停止し、偏
差が0になったら再スター・トすることができ、プログ
ラムを停止する偏差値は任意に設定することができる構
造となっている。本発明によれば、以上のように、布用
の染色条件に通した温度プログラムを自動的に得ること
ができるので、染めむら等の染色トラブルの発生しない
良好な結果が得られる。又、従来の経験的な方法に対し
条件が同じであれば、だれがやっても同じ結果が得られ
るので、品質のバラッキを無くすことができるので実用
上極めて有効である。以上はポリエステル100%の布
岳を分散染料を用いて染色加工する場合を例として温度
変化率の制御方法を説明したが、単に温度変化率ばかり
でなく、布の循環に関する以外の工程、たとえば染料や
薬品の注入工程等で泡立ち、液粘度変化等の染液条件が
不安定になり布岳の1循環時間が増加(布速度の低下)
した時には、染料や薬品の注入速度を遅くしたり、又最
大許容循環時間に達したとき染料、薬品等の注入を一時
停止させ、布帯の循環が再び許容循環時間内に戻ったの
を確認し、再度制御開始することも出来る。又上記の染
色加工の例を述べたが、その他に精練、漂白やたていま
立て(クレープ生成)等にも広く応用出来る。In FIG. 3, up to point a, the almost constant circulation time was t=60 seconds, but for some reason the value of t started to change. Then, the temperature increase rate from point b to point c is controlled by issuing a command to the temperature control device using the data obtained by calculating the sand with circulation time t = 6 from point a to point b using the formula. . Next, the circulation time from point b to point c is t = 69 sand, so when the detector 15 detects it at point c, the circulation time from point b to point c is calculated as t = 69. According to the data, the temperature control device operates from point c to point d.
This kind of operation is repeated, but if the allowable circulation time (overtime) t' is set, for example, in the case of Fig. 3, r=
7, the control of the temperature control device is stopped after the set time t' has elapsed, and the system waits until the next detector 15 issues a detection command. As described above, in addition to controlling the temperature change b rate using the calculation formula and using the one-cycle time of the cloth as a variable, there is another method that can be used to simply set the temperature program determined based on past experience. The temperature change rate is changed depending on the rate of increase/decrease in time. For example, one circulation time of a cloth band is 1%.
It is also possible to reduce the time-varying IB rate that has increased (reduced cloth speed) by 1%. Also, as described above, 1 of the cloth obi is automatically
In the method of setting a temperature program for each cycle, if for some reason the deviation between the measured value and the set value becomes large, such as not following the temperature set value, the program is stopped and restarted when the deviation becomes 0. The structure is such that the deviation value for stopping the program can be set arbitrarily. According to the present invention, as described above, it is possible to automatically obtain a temperature program that meets the dyeing conditions for cloth, so that good results can be obtained without dyeing problems such as uneven dyeing. In addition, compared to the conventional empirical method, if the conditions are the same, the same result can be obtained no matter who does it, so it is extremely effective in practice because it eliminates variations in quality. Above, we have explained how to control the temperature change rate by taking as an example the case where 100% polyester cloth is dyed using disperse dyes. The dye solution conditions become unstable due to foaming and changes in solution viscosity during the chemical injection process, etc., and the time for one circulation of Futake increases (decrease in fabric speed).
If this happens, slow down the injection speed of dyes or chemicals, or temporarily stop the injection of dyes or chemicals when the maximum allowable circulation time is reached, and check that the circulation of the fabric strip has returned to within the allowable circulation time. However, control can be started again. In addition, although the above-mentioned example of dyeing processing has been described, it can also be widely applied to other processes such as scouring, bleaching, and erecting (crepe formation).
即ち布岳の1循環時間t(秒)を変数とし、夫々の処理
の場合の計算式を与える。例えば T=K・t
……【BーT=K.f(t)+C
……【BrK・・・・・・・・・機械係数
f(t)・・・布岳の1循環時間tの函数C・・・・・
・・・・定数
更に布帯の1循環時間t(秒)を前述の方法で検知測定
する代りに、特許願N.昭55一102801(出願・
昭和53手7月25日)に述べた如く、布常が一定距離
夕を置いて設けられた一対の検出器の間を通過する時間
△tを検知測定して布速度vf=ごLニニtを演算で求
め、凶式或いはその他の処理計算式に代入して温度変化
率等を求め、処理温度や染料、薬品の注入速度等を制御
することが出来る。That is, one circulation time t (seconds) of Fugaku is used as a variable, and calculation formulas for each process are given. For example, T=K・t
...[B-T=K. f(t)+C
......[BrK......Mechanical coefficient f(t)...Function C of Futake's one circulation time t...
...Instead of detecting and measuring the constant and one circulation time t (seconds) of the cloth band in the above-mentioned method, patent application No. 1983-102801 (Application/
As mentioned in 1977 (July 25, 1972), the time △t for the cloth to pass between a pair of detectors placed a certain distance apart is detected and measured, and the cloth speed vf = 1. It is possible to calculate the rate of temperature change, etc. by calculating and substituting it into the formula or other processing calculation formula, and control the processing temperature, the injection rate of dyes, chemicals, etc.
この様にして本発明は染色以外の繊維処理に広く応用出
釆、染色加工の場合と同様に実用上極めて有効である。In this manner, the present invention is widely applicable to fiber treatments other than dyeing, and is extremely effective in practice as in the case of casting and dyeing.
第1図は本発明による無端状繊維製品の処理装贋の一実
施例を示す断面図、第2図は一般的なポリエステル繊維
の染色温度曲線、第3図は本発明の温度制御方法を示す
図である。
1・・・滞溜槽、2・・・移送管、6・・・ポンプ、9
・・・熱交換器、11・・・リール、12・・・彼処理
布岳、15・・・検出器、16・・・被測定体、19・
・・熱媒体入口、20・・・熱媒体出口。
が/物
が2函
が3麹Fig. 1 is a cross-sectional view showing an example of processing and fabrication of endless fiber products according to the present invention, Fig. 2 shows a dyeing temperature curve of a general polyester fiber, and Fig. 3 shows a temperature control method of the present invention. It is a diagram. 1... Retention tank, 2... Transfer pipe, 6... Pump, 9
... heat exchanger, 11 ... reel, 12 ... heat treatment cloth, 15 ... detector, 16 ... object to be measured, 19.
...heat medium inlet, 20...heat medium outlet. Ga/2 boxes of things are 3 koji
Claims (1)
せて処理する方法において、布帛の1循環時間を検知し
、あらかじめ設定された処理条件に基づき決められた温
度プログラムを、布帛の1循環時間が増加(布速度の低
下)した時には温度変化率を低減させ、その反対の時に
は逆となる様に変化に応じ、自動的に布帛の1循環ごと
に温度プログラムを修正することを特徴とする繊維製品
の処理方法。 2 繊維製品(以下布帛という)を無端状で循環回動さ
せて処理する方法において、布帛の1循環時間を検知し
、あらかじめ設定された処理条件に基づき決められた温
度プログラムを、布帛の1循環時間が増加(布速度の低
下)した時には温度変化率を低減させ、その反対の時に
は逆となる様に変化に応じ、自動的の布帛の1循環ごと
に温度プログラムを修正すると共に染料や薬品の注入速
度を制御するようにし、更に最大許容循環時間を設定し
、布帛の1循環が増大し、設定最大許容循環時間に達し
たとき前記染料、薬品の注入等を一時停止させ布帛の循
環が再び許容循環時間に戻つたのを確認し、再度制御を
開始することを特徴とする繊維製品の処理方法。 3 移送管と、滞溜槽と、これら移送管及び滞溜槽で形
成される環状の処理通路と、該通路中に設けられた上記
移送管の上流端に対する被処理布帛の送り込み手段と、
上記滞溜槽底部より循環ポンプを介して移送管の上流端
部に開口された噴射ノズルに通ずる処理液循環通路と、
該通路途中に介在された処理液の温度調節装置と、上記
環状の処理通路を移送される被処理布帛に付設した被測
定体と、これに対応する少なくとも1ケ以上の検知体と
、該検知体による測定結果を前記温度調節装置にフイー
ドバツクする手段を設けたことを特徴とする繊維製品の
処理装置。[Claims] 1. In a method of processing textile products (hereinafter referred to as fabric) by circulating them in an endless manner, one circulation time of the fabric is detected and a temperature program is determined based on preset processing conditions. When the fabric circulation time increases (fabric speed decreases), the temperature change rate is reduced, and vice versa.The temperature program is automatically corrected for each fabric circulation according to the change. A method for processing textile products, characterized by: 2. In a method of processing textile products (hereinafter referred to as fabric) by circulating them in an endless manner, one circulation time of the fabric is detected, and a temperature program determined based on preset processing conditions is applied to one cycle of the fabric. When time increases (fabric speed decreases), the rate of temperature change is reduced, and vice versa, the temperature program is modified for each automatic fabric cycle and dyes and chemicals are adjusted accordingly. The injection speed is controlled, and the maximum allowable circulation time is set, and when the number of cycles of fabric increases and the set maximum allowable circulation time is reached, the injection of the dye, chemical, etc. is temporarily stopped, and the circulation of the fabric is resumed. A method for processing textile products, characterized by starting control again after confirming that the circulation time has returned to an acceptable circulation time. 3. A transfer pipe, a retention tank, an annular processing passage formed by the transfer pipe and the retention tank, and means for feeding the fabric to be treated to the upstream end of the transfer pipe provided in the passage;
a processing liquid circulation passageway leading from the bottom of the retention tank to an injection nozzle opened at the upstream end of the transfer pipe via a circulation pump;
a temperature control device for the processing liquid interposed in the passage; a measuring object attached to the processed fabric being transferred through the annular processing passage; at least one sensing object corresponding thereto; 1. An apparatus for processing textile products, characterized in that it is provided with means for feeding back measurement results from the body to the temperature control apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17755981A JPS6030388B2 (en) | 1981-11-04 | 1981-11-04 | Processing method and device for textile products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17755981A JPS6030388B2 (en) | 1981-11-04 | 1981-11-04 | Processing method and device for textile products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5881667A JPS5881667A (en) | 1983-05-17 |
| JPS6030388B2 true JPS6030388B2 (en) | 1985-07-16 |
Family
ID=16033074
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17755981A Expired JPS6030388B2 (en) | 1981-11-04 | 1981-11-04 | Processing method and device for textile products |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6030388B2 (en) |
-
1981
- 1981-11-04 JP JP17755981A patent/JPS6030388B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5881667A (en) | 1983-05-17 |
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