JPH0518942B2 - - Google Patents
Info
- Publication number
- JPH0518942B2 JPH0518942B2 JP1304391A JP30439189A JPH0518942B2 JP H0518942 B2 JPH0518942 B2 JP H0518942B2 JP 1304391 A JP1304391 A JP 1304391A JP 30439189 A JP30439189 A JP 30439189A JP H0518942 B2 JPH0518942 B2 JP H0518942B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- drying
- textile product
- heater
- hot air
- 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 - Fee Related
Links
- 238000001035 drying Methods 0.000 claims description 83
- 239000004753 textile Substances 0.000 claims description 49
- 239000000835 fiber Substances 0.000 claims description 27
- 238000000034 method Methods 0.000 claims description 19
- 238000001704 evaporation Methods 0.000 claims description 17
- 230000008020 evaporation Effects 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 7
- 229920000742 Cotton Polymers 0.000 description 4
- 208000005156 Dehydration Diseases 0.000 description 4
- 230000006378 damage Effects 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 210000002268 wool Anatomy 0.000 description 4
- 235000013351 cheese Nutrition 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 241000220317 Rosa Species 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008041 oiling agent Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000009528 severe injury Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Treatment Of Fiber Materials (AREA)
- Drying Of Solid Materials (AREA)
Description
〔産業上の利用分野〕
本発明は、チーズ等のパツケージ繊維製品の乾
燥方法およびそれに用いる装置に関するものであ
る。
〔従来の技術〕
染色、水洗等の工程を経て濡れたチーズ等のパ
ツケージ繊維製品を乾燥する場合には、従来から
第5図に示すような装置が用いられている。この
装置は、送風機1と、加熱器2と、乾燥釡3と、
冷却器4とを備えており、上記送風機1から加熱
器2、乾燥釡3、冷却器4を経て再び上記送風機
1に戻る循環流路を循環する熱風によつて、上記
乾燥釡3内に装填したパツケージ繊維製品5の乾
燥を行うことができるようになつている。
上記乾燥釡3内における乾燥は、まず乾燥釡3
内を加圧して、パツケージの外側から内側に向か
つて圧力脱水する脱水工程と、熱風をパツケージ
の内側から外側に向かつて通過させることにより
繊維間の水分を蒸発させる乾燥工程と、乾燥がほ
ぼ完了した時点で熱風をパツケージの外側から内
側に向かつて通過させることにより調湿を行う調
湿工程とに分かれており、その進行は、作業者に
よつて予め設定された条件に従つて自動的に制御
されるようになつている。例えば、第6図に示す
ように、タイマーT1によつて予めセツトされた
所定時間だけ上記脱水が行われ(乾燥釡3内での
熱風の向きはパツケージの外側から内側方向)、
所定時間経過時点で切り換えコツクが作動して上
記熱風の向きが反対になるとともに脱水のための
加圧が解除される。そして、乾燥の進行とともに
パツケージ内の温度が上昇して水分の蒸発が充分
に進行した時点で、タイマーT2が作動し、予め
セツトされた所定時間経過後に切り換えコツクが
作動して再び乾燥釡3内での熱風の向きをパツケ
ージの外側から内側方向に変える。この状態で、
タイマーT3で定められる所定時間だけ上記調湿
工程が行われるようになつている。ただし、上記
3段階の工程が進行している間、乾燥釡3に送入
される熱風の温度は、一貫して一定の設定値とな
るよう制御されている。この制御は、加熱器2の
出口側に温度センサB(第5図参照)を設け、こ
の温度センサBの温度を常時一定の値Pに保つよ
う加熱器2を制御することによつて行われてい
る。なお、上記設定値Pは、乾燥対象となる繊維
製品5の種類、処理条件等によつて予め設定され
る。また、上記タイマーT2の作動開始は、具体
的には、乾燥釡3の出口側に設けられる温度セン
サX(第5図参照)によつて読み取られる乾燥器
出口温度が所定の温度Rに達した段階で作動指示
信号が発信されることによつて行われる。
〔発明が解決しようとする課題〕
しかしながら、このような乾燥方法では、繊維
間の水分を蒸発させる乾燥工程に要する時間が長
くかかるため、その時間短縮を図ることが重要な
課題となつている。これに対し、設定する熱風温
度を高くして乾燥を促進することも考えられる
が、従来から経験的に確立されている適正な熱風
温度よりも高い温度に設定すると、繊維製品が過
度の加熱を受けるため、糸に平滑性を与えるため
に含浸されているオイリング剤が焼けてオイリン
グ焼け現象を生じ、繊維表面が黄変して品質の低
下を招いたり、パツケージ化された糸を解舒する
際に糸捌きが悪くなつて糸表面が損傷するという
という問題があつた。
本発明は、このような事情に鑑みなされたもの
で、繊維製品にダメージを与えることなく乾燥時
間を短縮できるような繊維製品の乾燥方法および
その装置の提供をその目的とする。
〔課題を解決するための手段〕
上記の目的を達成するため、本発明は、送風機
から加熱器、乾燥釡、冷却器を経て再び上記送風
機に戻る循環流路を循環する熱風を、上記乾燥釡
内に装填したパツケージ繊維製品のパツケージ内
側から外側に向かつて通過させながら乾燥を行う
方法において、上記パツケージ繊維製品の繊維表
面からの水分蒸発が完了する時点を、パツケージ
繊維製品の内部温度を経時的に読み取る温度セン
サによつて読み取り、上記水分蒸発が完了する時
点までは、熱風の温度を、繊維製品に対する乾燥
の適正温度よりも高く設定し、上記水分蒸発が完
了する時点に達すると同時に、上記熱風の温度
を、繊維製品に対する乾燥の適正温度まで下げる
ようにしたパツケージ繊維製品の乾燥方法を第1
の要旨とし、送風機から加熱器、乾燥釡、冷却器
を経て再び上記送風機に戻る循環流路を循環する
熱風を、上記乾燥釡内に装填したパツケージ繊維
製品のパツケージ内側から外側に向かつて通過さ
せながら乾燥を行う装置において、上記パツケー
ジ繊維製品の内部温度を経時的に読み取る内部温
度センサAと、上記加熱器の出口側の熱風温度を
経時的に読み取る加熱器出口温度センサBと、乾
燥対象とする繊維製品の繊維表面からの水分蒸発
が完了する温度Sが予め入力される設定器Cと、
繊維製品に対する乾燥の適正温度Pと上記適正温
度よりも高い所定の温度Qの2種類の温度が予め
入力される設定器Dと、上記加熱器出口温度セン
サBによつて読み取られる加熱器出口温度が上記
設定器Dに入力された設定温度P,Qのいずれか
に一致するよう加熱器による熱風加熱を制御する
加熱制御手段と、上記設定器Cに入力された温度
Sと上記内部温度センサAによつて読み取られる
温度とを時々刻々比較し、両者が一致した時点で
加熱制御手段に温度変更指示を与える指示手段と
を備え、上記加熱器出口温度が、稼働開始から繊
維製品内部温度が上記設定温度Sに到達するまで
は、乾燥適正温度よりも高い温度Qと一致するよ
うに制御され、上記設定温度Sに到達すると同時
に、乾燥適正温度Pと一致するよう制御されるよ
うになつているパツケージ繊維製品の乾燥装置を
第2の要旨とする。
〔作用〕
すなわち、本発明者は、繊維製品が充分に加温
されていない濡れた状態では、熱風温度を従来か
ら適正温度とされてきた温度より高くしても、繊
維は損傷を受けず、繊維内の水分蒸発が促進され
るだけになるのではないか、との着想から一連の
研究を行つた。そして、繊維製品が充分に加温さ
れた時点をどのようにして判断すれば、最も効果
的に乾燥時間を短縮でき、しかも繊維製品の品質
を損なわないかについてさらに研究した。その結
果、パツケージ繊維製品の乾燥では、パツケージ
の内側から外側に向かつて熱風が通過してパツケ
ージの内側から乾燥が進行するのであり、内部に
おいて水分蒸発が進行している間は、繊維製品内
部の温度が殆ど上昇せず、内部に水分がなくなる
と急激に温度が上昇し、ついでパツケージ表面に
おける水分蒸発が即座に完了することがわかつ
た。このため、繊維製品のパツケージ表面の温度
を温度センサで経時的に読み取つてその上昇変化
を指標として熱風の温度制御を行うのでは、その
時点ですでにパツケージ内部では水分蒸発が完了
してしまつているので、熱風温度を下げるタイミ
ングが遅れて糸にダメージが生じてしまう。ま
た、乾燥釡内の温度変化や乾燥釡の出口側の熱風
温度の変化を読み取るのでは、一層上記タイミン
グが遅れて、糸の損傷がひどくなる。そこで、温
度センサを繊維製品内部に損入して繊維製品の内
部温度変化を経時的に読み取つてその上昇変化を
指標として熱風の温度制御を行うようにすれば、
繊維表面の水分蒸発の完了時点と熱風の温度変化
時点とがずれることなく、糸にダメージを与えな
い限界点まで高温熱風を与えることができること
を見いだし、本発明に到達した。
つぎに、本発明を実施例にもとづいて詳細に説
明する。
〔実施例〕
第1図は本発明の乾燥装置の一実施例を示して
いる。この乾燥装置は、従来の乾燥装置と同様、
送風機1と、加熱器2と、乾燥釡3と、冷却器4
とを備えており、上記送風機1から加熱器2、乾
燥釡3、冷却器4を経て再び上記送風機1に戻る
循環流路を循環する熱風によつて、上記乾燥釡3
内に装填したパツケージ繊維製品5の乾燥を行う
ことができるようになつている。また、加熱器2
の出口側に温度センサBが設けられ、乾燥釡3の
出口側に温度センサXが設けられている。さら
に、この装置では、第2図に示すように、上記パ
ツケージ繊維製品5の繊維内部にセンサ部が差し
込まれる内部温度センサAが設けられている。そ
して、これらの各温度センサA,B,Xのデータ
が経時的に読み取られ、脱水→乾燥→調湿という
段階的な進行が自動的に制御されるようになつて
いる。上記制御は、例えば第3図に示すような構
成を備えた制御盤10からの指示に従つて行われ
るようになつている。すなわち、上記制御盤10
には、乾燥対象とする繊維製品5の繊維表面から
の水分蒸発が完了する温度Sが予め入力される設
定器Cと、繊維製品5に対する乾燥の適正温度P
と上記適正温度Pよりも高い所定の温度Qの2種
類の温度が予め入力される設定器Dと、前記加熱
器出口温度センサBによつて読み取られる加熱器
出口温度が上記設定器Dに入力された設定温度
P,Qのいずれかに一致するよう加熱器2による
熱風加熱を制御する加熱制御手段11と、上記設
定器Cに入力された設定温度Sと前記繊維内に差
し込まれる内部温度センサAによつて読み取られ
る繊維内部温度とを時々刻々比較し両者が一致し
た時点で上記加熱制御手段11に温度変更指示を
与える指示手段12とが設けられている。なお、
上記繊維製品5の繊維表面からの水分蒸発が完了
する温度Sとは、乾燥の進行によつて繊維表面を
覆つていた水膜が蒸発して繊維が露出して加熱と
ともに繊維自体の内部温度が急上昇を開始する段
階の温度をいう。そして、この温度Sは、繊維の
種類、処理条件等にもとづいて予め上記設定器C
に入力される。また、上記繊維製品5に対する乾
燥の適正温度Pとは、従来から経験的に知られて
いる乾燥時の適正な熱風温度であつて、それ以上
の高温で乾燥を行うと最終的に繊維の損傷を引き
起こすとされる温度である。この温度も、繊維の
種類や処理条件等にもとづいて予め設定器Dに入
力される。例えば一般的な染色方法で得られた綿
製品であれば、P=105〜110℃、ウール製品であ
ればP=95〜100℃とされている。そして、上記
適正温度Pよりも高い所定温度Qとは、例えば
130〜135℃の温度をいう。
したがつて、この乾燥装置によれば、第4図に
示すように、内部温度センサAによつて読み取ら
れる繊維製品5の内部温度が、上記設定器Cに予
め入力された温度S(繊維製品の繊維表面からの
水分蒸発が完了する温度)に到達するまでは、加
熱器出口温度が、従来からの乾燥の適正温度Pよ
りも高い所定の温度Qになる乾燥条件で乾燥が行
われ、繊維製品の内部温度が上記設定器Cに予め
入力された温度Sに到達すると同時に、上記加熱
器出口温度が下がつて従来からの乾燥の適正温度
Pとなつて乾燥が続けられるようになつている。
他の制御方法は、従来と同様であり、構成および
動作の説明は省略する。
このように、上記乾燥装置によれば、繊維製品
5の繊維表面からの水分蒸発が完了するまでの乾
燥を、従来の乾燥適正温度Pよりも高い温度Qで
行うため、繊維製品5が上記水分蒸発完了状態に
到達するまでの時間を大幅に短縮することができ
る。そして、この状態に到達した時点を、パツケ
ージの繊維内部の温度変化で検知し、内部での水
分蒸発完了後、即座に加熱温度を従来の乾燥適正
温度Pまで下げるため、それ以降の乾燥は、従来
と同様隠やかな条件での乾燥となり、繊維の損傷
を引き起こすことがない。
つぎに、綿糸およびウール糸のそれぞれについ
て、上記の方法および従来法に従つて乾燥を行つ
た。乾燥条件および所要時間は下記の第1表およ
び第2表に示すとおりである。また、得られたパ
ツケージ製品の糸を解舒してその品質を評価し、
その結果を併せて示した。
〈綿糸を用いた場合〉
糸 種 綿100%
太 さ 30/1
糸 量 158Kg
[Industrial Application Field] The present invention relates to a method for drying packaged fiber products such as cheese and an apparatus used therefor. [Prior Art] When drying a packaged textile product such as cheese that has been wet after dyeing, washing, etc., an apparatus as shown in FIG. 5 has conventionally been used. This device includes a blower 1, a heater 2, a drying pot 3,
The drying pot 3 is loaded with hot air that circulates through a circulation path from the blower 1, through the heater 2, the drying pot 3, the cooler 4, and back to the blower 1. The packaged textile product 5 can be dried. Drying in the drying pot 3 is first carried out in the drying pot 3.
The dehydration process involves pressurizing the inside of the package and dehydrating it from the outside to the inside, and the drying process involves passing hot air from the inside of the package to the outside to evaporate the moisture between the fibers. Drying is almost complete. At this point, the process is divided into a humidity control process in which the humidity is controlled by passing hot air from the outside to the inside of the package cage. It's becoming controlled. For example, as shown in FIG. 6, the dehydration is performed for a predetermined period of time preset by the timer T1 (the direction of the hot air in the drying pot 3 is from the outside to the inside of the package),
After a predetermined period of time has elapsed, a switching mechanism is operated to reverse the direction of the hot air and release pressure for dehydration. Then, as the drying progresses, the temperature inside the package rises and when the moisture has sufficiently evaporated, the timer T2 is activated, and after a preset period of time has elapsed, the switching pot is activated and the drying pot 3 is turned on again. Change the direction of hot air inside from the outside of the package cage to the inside. In this state,
The humidity control process is performed for a predetermined time determined by a timer T3 . However, while the above-mentioned three-stage process is progressing, the temperature of the hot air sent into the drying pot 3 is consistently controlled to be a constant set value. This control is performed by providing a temperature sensor B (see Figure 5) on the outlet side of the heater 2 and controlling the heater 2 so that the temperature of this temperature sensor B is always maintained at a constant value P. ing. Note that the set value P is set in advance depending on the type of textile product 5 to be dried, processing conditions, etc. In addition, the operation of the timer T2 starts when the dryer outlet temperature, which is read by the temperature sensor This is done by transmitting an operation instruction signal at this stage. [Problems to be Solved by the Invention] However, in such a drying method, the time required for the drying step to evaporate the moisture between the fibers is long, so it is an important problem to shorten the time. On the other hand, it is possible to accelerate drying by setting the hot air temperature higher, but if the temperature is set higher than the appropriate hot air temperature that has been empirically established, textile products will not be heated excessively. Due to this, the oiling agent impregnated to give the thread smoothness burns, causing oiling burn phenomenon, which yellows the fiber surface and causes a decrease in quality. Another problem was that the thread handling became poor and the thread surface was damaged. The present invention was made in view of the above circumstances, and an object of the present invention is to provide a method and apparatus for drying textile products that can shorten the drying time without damaging the textile products. [Means for Solving the Problems] In order to achieve the above object, the present invention provides hot air that circulates through a circulation channel from a blower through a heater, a drying pot, a cooler, and back to the blower, to the drying pot. In a method of drying a packaged textile product loaded in a package by passing it from the inside to the outside, the internal temperature of the packaged textile product is determined over time to determine the point at which moisture evaporation from the fiber surface of the packaged textile product is completed. The temperature of the hot air is set higher than the appropriate drying temperature for the textile product until the moisture evaporation is completed, as read by a temperature sensor read by a temperature sensor, and as soon as the moisture evaporation is completed, the hot air is heated. The first method of drying packaged textile products is to reduce the temperature of hot air to the appropriate temperature for drying textile products.
The gist of this is that hot air circulates through a circulation path from the blower through the heater, drying kettle, cooler, and back to the blower, and passes from the inside of the package cage of the packaged textile product loaded in the drying pot to the outside. The apparatus includes an internal temperature sensor A that reads the internal temperature of the packaged textile product over time, a heater outlet temperature sensor B that reads the hot air temperature on the exit side of the heater over time, and a heater outlet temperature sensor B that reads the temperature of the hot air on the outlet side of the heater over time. a setting device C into which a temperature S at which moisture evaporation from the fiber surface of the textile product is completed is input in advance;
A setting device D into which two types of temperatures, an appropriate drying temperature P for textile products and a predetermined temperature Q higher than the above-mentioned appropriate temperature, are input in advance, and a heater outlet temperature read by the heater outlet temperature sensor B. a heating control means for controlling hot air heating by the heater so that the temperature matches either the set temperature P or Q inputted to the setting device D, and the temperature S inputted to the setting device C and the internal temperature sensor A; and an instruction means for momentarily comparing the temperature read by the heater and the temperature read by the heater, and instructing the heating control means to change the temperature when the two match, so that the temperature at the outlet of the heater is equal to the temperature inside the textile product from the start of operation. Until the set temperature S is reached, the temperature is controlled to match the temperature Q higher than the proper drying temperature, and as soon as the set temperature S is reached, the temperature is controlled to match the proper drying temperature P. The second gist is a drying device for packaged textile products. [Function] In other words, the present inventor has found that in a wet state where the textile product has not been sufficiently heated, even if the hot air temperature is higher than the temperature that has conventionally been considered to be an appropriate temperature, the fiber will not be damaged. We conducted a series of studies based on the idea that this might simply accelerate the evaporation of water within the fibers. They then conducted further research on how to determine when textile products have been sufficiently warmed to most effectively shorten drying time without impairing the quality of the textile products. As a result, when drying packaged textile products, hot air passes from the inside of the package to the outside, and drying progresses from the inside of the package. It was found that the temperature hardly rose, and when there was no moisture inside, the temperature rose rapidly, and then the evaporation of moisture on the surface of the package was completed immediately. For this reason, if the temperature on the surface of the package of textile products is read over time with a temperature sensor and the temperature of the hot air is controlled using the increase in temperature as an indicator, the moisture evaporation inside the package will have already been completed at that point. As a result, the timing of lowering the hot air temperature is delayed, causing damage to the yarn. Furthermore, reading the temperature change inside the drying kettle or the change in the temperature of the hot air on the outlet side of the drying kettle delays the above-mentioned timing even further, resulting in severe damage to the yarn. Therefore, if a temperature sensor is inserted inside the textile product to read the internal temperature change of the textile product over time, and the temperature of the hot air is controlled using the rising change as an indicator,
The inventors have discovered that it is possible to apply high-temperature hot air to the limit without damaging the yarn, without causing a lag between the time when moisture evaporation on the fiber surface is completed and the time when the temperature of the hot air changes, and the present invention has been achieved. Next, the present invention will be explained in detail based on examples. [Embodiment] FIG. 1 shows an embodiment of the drying apparatus of the present invention. This drying device is similar to conventional drying devices,
Blower 1, heater 2, drying pot 3, cooler 4
The drying pot 3 is heated by the hot air circulating in the circulation channel from the blower 1 through the heater 2, the drying pot 3, the cooler 4, and back to the blower 1.
The package textile product 5 loaded therein can be dried. Also, heater 2
A temperature sensor B is provided on the exit side of the drying pot 3, and a temperature sensor X is provided on the exit side of the drying pot 3. Furthermore, this device is provided with an internal temperature sensor A whose sensor section is inserted into the fibers of the packaged textile product 5, as shown in FIG. Data from each of these temperature sensors A, B, and X is read over time, and the stepwise progression of dehydration→drying→humidity control is automatically controlled. The above control is performed in accordance with instructions from a control panel 10 having a configuration as shown in FIG. 3, for example. That is, the control panel 10
, there is a setting device C in which the temperature S at which moisture evaporation from the fiber surface of the textile product 5 to be dried is completed is input in advance, and an appropriate temperature P for drying the textile product 5.
and a predetermined temperature Q higher than the appropriate temperature P are input in advance to the setting device D; and the heater outlet temperature read by the heater outlet temperature sensor B is input to the setting device D. a heating control means 11 for controlling the hot air heating by the heater 2 so as to match either the set temperature P or Q set by the controller C; and a set temperature S input to the setter C and an internal temperature sensor inserted into the fiber. An instruction means 12 is provided which momentarily compares the fiber internal temperature read by A and gives a temperature change instruction to the heating control means 11 when the two match. In addition,
The temperature S at which moisture evaporation from the fiber surface of the textile product 5 is completed means that as drying progresses, the water film covering the fiber surface evaporates, the fiber is exposed, and the internal temperature of the fiber itself increases as the fiber is heated. This is the temperature at which the temperature begins to rise rapidly. This temperature S is set in advance using the setting device C based on the type of fiber, processing conditions, etc.
is input. Further, the appropriate temperature P for drying the textile product 5 is the appropriate hot air temperature for drying that has been known empirically, and drying at a higher temperature will eventually damage the fibers. This is the temperature that is said to cause This temperature is also input in advance to the setting device D based on the type of fiber, processing conditions, etc. For example, for cotton products obtained by general dyeing methods, P is set to be 105 to 110°C, and for wool products, P is set to be 95 to 100°C. The predetermined temperature Q higher than the appropriate temperature P is, for example,
Refers to a temperature of 130-135℃. Therefore, according to this drying device, as shown in FIG. 4, the internal temperature of the textile product 5 read by the internal temperature sensor A is the temperature S (textile product Until reaching the temperature at which moisture evaporation from the fiber surface is completed, drying is performed under drying conditions in which the heater outlet temperature is a predetermined temperature Q higher than the conventional appropriate drying temperature P. At the same time that the internal temperature of the product reaches the temperature S input in advance into the setting device C, the outlet temperature of the heater decreases to the conventional appropriate temperature P for drying, and drying can be continued. .
Other control methods are the same as conventional ones, and explanations of the configuration and operation will be omitted. As described above, according to the above drying device, drying is performed at a temperature Q higher than the conventional appropriate drying temperature P until the moisture evaporation from the fiber surface of the textile product 5 is completed. The time required to reach the evaporation completion state can be significantly shortened. Then, the point at which this state is reached is detected by the temperature change inside the fibers of the package, and after the moisture evaporation inside is completed, the heating temperature is immediately lowered to the conventional appropriate drying temperature P. Drying is carried out under the same conditions as before, so there is no damage to the fibers. Next, each of the cotton yarn and wool yarn was dried according to the above method and a conventional method. The drying conditions and required time are as shown in Tables 1 and 2 below. In addition, we unwound the yarn of the obtained package product and evaluated its quality.
The results are also shown. <When using cotton thread> Thread type 100% cotton Thickness 30/1 Thread amount 158Kg
【表】 〈ウール糸を用いた場合〉 糸 種 ウール100% 太 さ 52/2 糸 量 166Kg【table】 <When using wool yarn> Thread type: 100% wool Thickness 52/2 Thread amount 166Kg
以上のように、本発明のパツケージ繊維製品の
乾燥方法によれば、従来困難とされていた乾燥時
間の大幅な短縮を、繊維製品の変色や糸捌き不良
等の損傷を招くことなく達成することができる。
また、本発明の乾燥装置によれば、従来の乾燥装
置に簡単な改良を施すだけで、上記方法を簡単に
実施することができる。
As described above, according to the method for drying packaged textile products of the present invention, it is possible to significantly shorten the drying time, which has been considered difficult in the past, without causing damage to the textile products such as discoloration or poor yarn handling. I can do it.
Further, according to the drying device of the present invention, the above method can be easily carried out by simply making improvements to the conventional drying device.
第1図は本発明の乾燥装置の一実施例を示す構
成図、第2図は上記実施例に用いる内部温度セン
サの取り付け態様の詳細説明図、第3図は上記実
施例に用いる制御盤の構成図、第4図は上記実施
例の工程の進行に伴う各部分の温度変化を示す線
図、第5図は従来の乾燥装置の一例を示す構成
図、第6図は上記従来例の工程の進行に伴う各部
分の温度変化を示す線図である。
1…送風機、2…加熱器、3…乾燥釡、4…冷
却器、5…繊維製品、10…制御盤、11…加熱
制御手段、12…指示手段、A,X…温度セン
サ、C,D…設定器。
Fig. 1 is a configuration diagram showing one embodiment of the drying apparatus of the present invention, Fig. 2 is a detailed explanatory diagram of the manner in which the internal temperature sensor used in the above embodiment is attached, and Fig. 3 is a diagram showing the control panel used in the above embodiment. 4 is a diagram showing the temperature change of each part as the process of the above embodiment progresses; FIG. 5 is a block diagram showing an example of a conventional drying device; and FIG. 6 is a diagram showing the process of the above conventional example. FIG. 3 is a diagram showing temperature changes in each part as the process progresses. DESCRIPTION OF SYMBOLS 1...Blower, 2...Heater, 3...Drying pot, 4...Cooler, 5...Textile product, 10...Control panel, 11...Heating control means, 12...Instruction means, A, X...Temperature sensor, C, D ...Setting device.
Claims (1)
び上記送風機に戻る循環流路を循環する熱風を、
上記乾燥釡内に装填したパツケージ繊維製品のパ
ツケージ内側から外側に向かつて通過させながら
乾燥を行う方法において、上記パツケージ繊維製
品の繊維表面からの水分蒸発が完了する時点を、
パツケージ繊維製品の内部温度を経時的に読み取
る温度センサによつて読み取り、上記水分蒸発が
完了する時点までは、熱風の温度を、繊維製品に
対する乾燥の適正温度よりも高く設定し、上記水
分蒸発が完了する時点に達すると同時に、上記熱
風の温度を、繊維製品に対する乾燥の適正温度ま
で下げるようにしたことを特徴とするパツケージ
繊維製品の乾燥方法。 2 送風機から加熱器、乾燥釡、冷却器を経て再
び上記送風機に戻る循環流路を循環する熱風を、
上記乾燥釡内に装填したパツケージ繊維製品のパ
ツケージ内側から外側に向かつて通過させながら
乾燥を行う装置において、上記パツケージ繊維製
品の内部温度を経時的に読み取る内部温度センサ
Aと、上記加熱器の出口側の熱風温度を経時的に
読み取る加熱器出口温度センサBと、乾燥対象と
する繊維製品の繊維表面からの水分蒸発が完了す
る温度Sが予め入力される設定器Cと、繊維製品
に対する乾燥の適正温度Pと上記適正温度よりも
高い所定の温度Qの2種類の温度が予め入力され
る設定器Dと、上記加熱器出口温度センサBによ
つて読み取られる加熱器出口温度が上記設定器D
に入力された設定温度P,Qのいずれかに一致す
るよう加熱器による熱風加熱を制御する加熱制御
手段と、上記設定器Cに入力された温度Sと上記
内部温度センサAによつて読み取られる温度とを
時々刻々比較し、両者が一致した時点で加熱制御
手段に温度変更指示を与える指示手段とを備え、
上記加熱器出口温度が、稼動開始から繊維製品内
部温度が上記設定温度Sに到達するまでは、乾燥
適正温度よりも高い温度Qと一致するように制御
され、上記設定温度Sに到達すると同時に、乾燥
適正温度Pと一致するよう制御されるようになつ
ていることを特徴とするパツケージ繊維製品の乾
燥装置。[Scope of Claims] 1. Hot air that circulates through a circulation channel from an air blower through a heater, a drying pot, a cooler, and then back to the air blower,
In the method of drying the packaged textile product loaded in the drying kettle while passing it from the inside of the package to the outside, the point at which water evaporation from the fiber surface of the packaged textile product is completed is
The internal temperature of the packaged textile product is read by a temperature sensor that reads over time, and the temperature of the hot air is set higher than the appropriate drying temperature for the textile product until the moisture evaporation is completed. A method for drying a packaged textile product, characterized in that the temperature of the hot air is lowered to an appropriate temperature for drying the textile product as soon as the drying process reaches the point of completion. 2. Hot air circulates through a circulation path from the blower through the heater, drying pot, cooler, and back to the blower.
The apparatus for drying the packaged textile product loaded in the drying pot while passing the packaged textile product from the inside of the package to the outside includes an internal temperature sensor A that reads the internal temperature of the packaged textile product over time, and an outlet of the heater. A heater outlet temperature sensor B that reads the hot air temperature on the side over time, a setting device C that inputs in advance the temperature S at which moisture evaporation from the fiber surface of the textile product to be dried is completed, and There is a setting device D into which two types of temperatures, a proper temperature P and a predetermined temperature Q higher than the proper temperature, are input in advance, and a setting device D in which the heater outlet temperature read by the heater outlet temperature sensor B is input.
heating control means for controlling the hot air heating by the heater to match either of the set temperatures P or Q inputted in the setting device C; and an instruction means that compares the temperature from time to time and gives a temperature change instruction to the heating control means when the two match,
The heater outlet temperature is controlled to match a temperature Q higher than the appropriate drying temperature from the start of operation until the internal temperature of the textile product reaches the set temperature S, and at the same time when the temperature reaches the set temperature S, A drying device for packaged textile products, characterized in that the drying temperature is controlled to match a suitable drying temperature P.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30439189A JPH03167365A (en) | 1989-11-22 | 1989-11-22 | Drying of packaged textile goods and equipment used therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30439189A JPH03167365A (en) | 1989-11-22 | 1989-11-22 | Drying of packaged textile goods and equipment used therefor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03167365A JPH03167365A (en) | 1991-07-19 |
JPH0518942B2 true JPH0518942B2 (en) | 1993-03-15 |
Family
ID=17932456
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30439189A Granted JPH03167365A (en) | 1989-11-22 | 1989-11-22 | Drying of packaged textile goods and equipment used therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03167365A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06102866B2 (en) * | 1992-03-23 | 1994-12-14 | 株式会社日阪製作所 | Method and device for drying packaged textile products |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5314851A (en) * | 1976-07-27 | 1978-02-09 | Tsudakoma Ind Co Ltd | Hottair drying method of starched thread |
JPS63286188A (en) * | 1987-05-18 | 1988-11-22 | 松下電器産業株式会社 | Clothing drying apparatus |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5957791U (en) * | 1982-10-08 | 1984-04-14 | 株式会社日阪製作所 | High pressure drying equipment |
JPH0316638Y2 (en) * | 1988-01-06 | 1991-04-09 |
-
1989
- 1989-11-22 JP JP30439189A patent/JPH03167365A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5314851A (en) * | 1976-07-27 | 1978-02-09 | Tsudakoma Ind Co Ltd | Hottair drying method of starched thread |
JPS63286188A (en) * | 1987-05-18 | 1988-11-22 | 松下電器産業株式会社 | Clothing drying apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH03167365A (en) | 1991-07-19 |
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