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JPS5812363B2 - Boiled cocoon method - Google Patents

Boiled cocoon method

Info

Publication number
JPS5812363B2
JPS5812363B2 JP8641081A JP8641081A JPS5812363B2 JP S5812363 B2 JPS5812363 B2 JP S5812363B2 JP 8641081 A JP8641081 A JP 8641081A JP 8641081 A JP8641081 A JP 8641081A JP S5812363 B2 JPS5812363 B2 JP S5812363B2
Authority
JP
Japan
Prior art keywords
cocoon
water
boiling
tank
steaming
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
Application number
JP8641081A
Other languages
Japanese (ja)
Other versions
JPS57191314A (en
Inventor
岡田薫
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 JP8641081A priority Critical patent/JPS5812363B2/en
Publication of JPS57191314A publication Critical patent/JPS57191314A/en
Publication of JPS5812363B2 publication Critical patent/JPS5812363B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は煮繭方法に関するものであり、更に詳しくは、
蒸煮部の圧力状態を大気圧未満の負圧状態とした煮繭方
法に関するものである。
[Detailed Description of the Invention] The present invention relates to a cocoon boiling method, and more specifically,
This invention relates to a cocoon boiling method in which the pressure state of the steaming section is set to a negative pressure state below atmospheric pressure.

生糸製造工程においては、繰糸前の繭に水と熱エネルギ
ーを同時に与え、繭層繭糸のセリシン粒子間の結合を弱
めこれを膨潤溶解せしめて膠着度を減じ、繰糸を可能な
らしめるための熱水処理を施すものであり、これを行う
のに煮繭機を用いている。
In the raw silk manufacturing process, hot water is applied simultaneously to the cocoons before reeling, weakening the bonds between sericin particles in the cocoon layer and causing them to swell and dissolve, reducing the degree of stickiness and making reeling possible. A cocoon boiling machine is used for this purpose.

原料繭は貯繭中においても輛体に無水量の12係程度、
繭層に無水量の11%以下の水分を含有して乾燥状態を
保つでおり、繭を煮繭湯内に直接入れて煮繭したのでは
、繭は一部分のみ煮繭湯と接触するのみで均一な煮熟は
得難い、従って先ず繭層繊維間特に繭腔内の空気を排除
し、之を水に置換してこの水を通して煮繭湯の熱エネル
ギーを繭層セリシンに与え軟化膨潤を計る必要がある。
The raw material cocoon has about 12 parts of anhydrous water in its body even during storage.
The cocoon layer contains less than 11% of the anhydrous amount of water to maintain a dry state, and if the cocoon is placed directly into the boiling cocoon water and boiled, only a portion of the cocoon will come into contact with the boiling water. Uniform boiling is difficult to achieve, so it is necessary to first eliminate the air between the fibers of the cocoon layer, especially within the cocoon cavity, replace it with water, and pass through this water to apply the thermal energy of the boiling water to the sericin of the cocoon layer to soften and swell the cocoon layer. There is.

この様なことから、煮繭機内各工程での技術的課題は、
煮繭前処理(浸漬部、触蒸部、滲透部)における繭層へ
の均一施水と、蒸煮部における繭腔内空気の完全脱気が
挙げられる。
For this reason, the technical issues in each process within the cocoon boiling machine are as follows:
These include the uniform application of water to the cocoon layer in the cocoon pre-treatment (immersion section, steaming section, permeation section) and complete deaeration of the air inside the cocoon cavity in the steaming section.

前処理における問題点を更に考察すると、一層1は第1
図の如く、粗の部分2と密の部分3から形成されており
、密の部分3は粗の部分2より通水性に欠けている。
If we further consider the problems in preprocessing, the first
As shown in the figure, it is formed of a coarse portion 2 and a dense portion 3, with the dense portion 3 having less water permeability than the coarse portion 2.

本来密の部分3こそ熟度をすすめる必要から早く吸水し
て欲しいにもかゝわらず、実際には逆で粗の部分2が先
にぬれて、その結果熟成斑を起生している。
Although it is originally the dense part 3 that should absorb water quickly because it is necessary to promote ripeness, in reality it is the opposite and the coarse part 2 gets wet first, resulting in ripening spots.

従来公知の煮繭方法においては、密の部分3まで充分吸
水せしめる方法として、 (a)90〜95℃の高混水を用いて繭層全体へ熱湯を
滲透させる。
In the conventionally known cocoon boiling method, as a method for sufficiently absorbing water up to the dense part 3, (a) boiling water is permeated into the entire cocoon layer using highly mixed water at 90 to 95°C.

(b) 滲透剤を用いて水の表面張力を極端に下げる
ことにより繭層に均一に吸水させる。
(b) By extremely lowering the surface tension of water using a penetrating agent, the cocoon layer absorbs water uniformly.

(c)空気圧の変化で吸水させる。(c) Water is absorbed by changes in air pressure.

3方法の内、いずれかが採用されている。One of the three methods has been adopted.

しかしながら前記(a)方法で繭層への吸水を計ると、
次の蒸煮部における繭腔4の脱気が妨げられ浮き繭とな
る傾向が増大して好ましくなく、又(b)方法は薬剤濃
度を可成り高めなければその効果が期待出来ず実用性に
乏しく、又(C)方法は吸水効果に限界がある。
However, when measuring water absorption into the cocoon layer using method (a) above,
This is undesirable because the deaeration of the cocoon cavity 4 in the next steaming section is hindered and the tendency to form floating cocoons increases, and method (b) is not practical because it cannot be expected to be effective unless the drug concentration is considerably increased. In addition, method (C) has a limited water absorption effect.

この様に従来公知の方法はいずれも完全なものではなく
、更に考究すると、前処理が不適切であるとかえって煮
熟斑を大きくする危険性がある。
As described above, none of the conventionally known methods is perfect, and upon further consideration, there is a risk that inappropriate pretreatment may actually increase the size of boiling spots.

又蒸煮部での繭状態を考察すると、繭腔4への吸水を計
り沈繰煮繭が可能な様にするためには、一時飽和蒸気で
満した室内を通過させ、繭腔4内の空気を蒸気に置き換
える必要があり、蒸気に置換した後、直ちに100℃以
下の熱湯中に沈めることにより初めて100%に近い吸
水を完了するのであるが、繭の種類によっては100℃
の熱湯に繭層を接触させることを避け、100℃以下の
例えば98℃或は96℃で煮繭を完了したい場合がある
Considering the state of the cocoon in the steaming section, in order to measure the water absorption into the cocoon cavity 4 and make it possible to boil the cocoon by sinking, the cocoon must be passed through a chamber temporarily filled with saturated steam, and the air inside the cocoon cavity 4 must be It is necessary to replace the cocoon with steam, and after replacing it with steam, it is necessary to immediately submerge it in hot water below 100°C to complete nearly 100% water absorption.
There are cases where it is desired to avoid contacting the cocoon layer with hot water and complete the cocoon boiling at a temperature below 100°C, for example 98°C or 96°C.

ところが現在公知の煮繭機においては、先に述べた前処
理過程での煮熟斑を解消するためにも又繭腔内空気の脱
気を計るためにも、100°Cの熱湯に一度は繭を接触
させざるを得ない構造である。
However, in the currently known cocoon boiling machine, the cocoon is soaked in boiling water at 100°C once in order to eliminate the boiling spots during the pretreatment process mentioned above and also to deaerate the air inside the cocoon cavity. This structure forces the cocoons to come into contact with each other.

従って実際の操業に当ってはかゝる要求を満すため、繭
が浮かないぎりぎりの温度を用いて煮繭を行っており、
温度制御に多大の苦心を要すると共に、調整範囲の狭少
による不完全煮繭が頻発しているのである。
Therefore, in order to meet these requirements during actual operations, the cocoons are boiled at the lowest possible temperature at which the cocoons do not float.
Temperature control requires a great deal of effort, and incomplete cocooning frequently occurs due to the narrow adjustment range.

本発明の目的は従来の煮繭方法が有するこの様な欠点を
解消せんとするもので、蒸煮部の圧力を所定の負圧に制
御するようになし該部の調整圧に応じて処理水の沸点を
替え、これにより適正温度下の熟成を斑なく完了させる
ことを特徴とするもので、少くとも前処理工程、蒸煮工
程、調整工程を順次経由せしめる連続煮繭方法において
、前処理工程により浸漬及び滲透処理を受けた繭粒を、
飽和蒸気が充満し且つ大気圧未満の所定負圧に保たれた
蒸煮室に通し、引き続いて前記蒸煮室に密接する調整槽
上部の100℃未満の煮繭水に没入させ、繭粒移送方向
に向って順次圧力を高め、大気圧に達する前記煮繭水を
経由せしめて煮繭することを要旨とするものである。
The purpose of the present invention is to eliminate such drawbacks of the conventional cocoon boiling method, and the pressure of the steaming section is controlled to a predetermined negative pressure, and the treated water is adjusted according to the adjusted pressure of the section. It is characterized by changing the boiling point and thereby completing the ripening at an appropriate temperature uniformly.In a continuous cocoon boiling method that sequentially passes through at least a pretreatment process, a steaming process, and an adjustment process, the pretreatment process and cocoon grains that have undergone percolation treatment,
The cocoons are passed through a steaming chamber filled with saturated steam and maintained at a predetermined negative pressure below atmospheric pressure, and then immersed in boiled cocoon water at a temperature of less than 100°C in the upper part of a regulating tank that is in close contact with the steaming chamber, in the direction of cocoon grain transfer. The gist of this method is to gradually increase the pressure and boil the cocoons through the boiled cocoon water that reaches atmospheric pressure.

以下第2図に示す実施例により本発明方法を具体的に説
明する。
The method of the present invention will be specifically explained below using an example shown in FIG.

先づ最初に実施装置の構成を説明する。First, the configuration of the implementation device will be explained.

第2図において、5は複数個の繭容器(図示しない)を
適宜間隔に取付けた無端鎖を示すもので、矢印方向に巡
回走行しており、該無端鎖5の走行路には順次煮繭機の
浸漬部である浸漬槽6、触蒸部である触蒸室7、滲透部
である滲透槽8、蒸煮部である蒸煮室9、調整部である
調整槽10を配設している。
In FIG. 2, reference numeral 5 indicates an endless chain to which a plurality of cocoon containers (not shown) are attached at appropriate intervals, and the endless chain 5 travels in the direction of the arrow. The machine is provided with an immersion tank 6 as an immersion section, an catalytic chamber 7 as an evaporation section, a permeation tank 8 as a permeation section, a steaming chamber 9 as a steaming section, and an adjustment tank 10 as an adjustment section.

浸漬槽6は約70℃の温水を貯留する湯槽からなり、無
端鎖5によって巡回する繭容器を充分浸漬する用をなす
と共に、次に位置する触蒸室7の蒸気を湯水でシールす
る用をなしており、又触蒸室7は浸漬槽6と滲透槽8の
湯水でシールされたほゞ70℃の蒸気室からなり、供気
口11より蒸気を供給され、余剰蒸気を浸漬槽6の水面
を通して外部へ放出し、又ドレンは次に位置する滲透槽
8へ放出する構造になっている。
The immersion tank 6 consists of a hot water tank that stores hot water at about 70°C, and is used to sufficiently immerse the cocoon containers circulated by the endless chain 5, and to seal the steam in the catalytic chamber 7 located next with hot water. The vaporization chamber 7 consists of a steam chamber at approximately 70°C sealed with hot water from the immersion tank 6 and the permeation tank 8. Steam is supplied from the air supply port 11, and excess steam is drained from the immersion tank 6. The drain is discharged to the outside through the water surface, and the drain is discharged to the seepage tank 8 located next.

該滲透槽8は約70℃の温水を貯留する水槽からなり、
先に述べた様に触蒸室7の蒸気シールの用をなす構造で
ある。
The seepage tank 8 consists of a water tank that stores warm water at about 70°C,
As mentioned earlier, this structure serves as a steam seal for the vaporization chamber 7.

しかして、実施例の煮繭機は前記浸漬槽6、触蒸室7、
滲透槽8により蒸煮前の前処理工程用槽を形成している
Therefore, the cocoon boiling machine of the embodiment includes the soaking tank 6, the contact chamber 7,
The seepage tank 8 forms a tank for a pretreatment process before steaming.

次いで蒸煮室9周辺の構造を説明すると、図に示す通り
、蒸煮室9は略々倒立U字形に形成された閉塞槽内の最
上部に形成されており、該閉塞槽の繭容器の入口側には
繭容器進行路をV字形とした水槽が密接し、又出口側に
はV字形管体に形成された調整槽10が密接している。
Next, the structure around the steaming chamber 9 will be explained. As shown in the figure, the steaming chamber 9 is formed at the top of a closed tank formed in an approximately inverted U shape, and the inlet side of the cocoon container of the closed tank is A water tank with a V-shaped cocoon container traveling path is in close contact with the cocoon container, and an adjustment tank 10 formed in a V-shaped tube body is in close contact with the outlet side.

しかして前記蒸煮室9は公知の減圧装置12に接続し、
該装置12の作用により蒸煮室9を大気圧以下の負圧状
態となしており、又蒸煮室9人口の水槽及び調整槽10
には夫々空気シール用の湯水が貯留し、且つ両槽の開口
端は大気中に開口している。
Thus, the steaming chamber 9 is connected to a known pressure reducing device 12,
By the action of the device 12, the steaming chamber 9 is brought into a negative pressure state below atmospheric pressure, and the steaming chamber 9 has a water tank and an adjustment tank 10.
Hot water for air sealing is stored in each tank, and the open ends of both tanks are open to the atmosphere.

従って両槽の水位は蒸煮室9の負圧状態に応じて第2図
図示の如き水位となる。
Therefore, the water levels in both tanks become as shown in FIG. 2 depending on the negative pressure state of the steaming chamber 9.

調整用の湯水を収容する調整槽10は又蒸気供給パルプ
13に接続しており、操業時、供給蒸気によって沸騰状
態となり、又その上部に位置する蒸煮室9は飽和蒸気で
充満した状態となる。
The adjustment tank 10 containing hot water for adjustment is also connected to the steam supply pulp 13, and during operation, the supplied steam brings it into a boiling state, and the steaming chamber 9 located above it is filled with saturated steam. .

本発明方法は上述の様な構造からなる装置を用いて実施
するもので、繭は無端鎖5に取付けられた繭容器内の図
上A点で投入され、公知の進行式煮繭機と同様、繭容器
に収容されたまへ無端鎖の進行につれて連続的に浸漬槽
6、触蒸室7、滲透槽8を通り、各部の処理及び蒸気の
作用を受け、先に記載の如く繭層内への吸水を計りなか
ら蒸煮室9及び調整槽10へ達する。
The method of the present invention is carried out using an apparatus having the above-described structure, and the cocoons are put into the cocoon container attached to the endless chain 5 at point A in the figure, similar to the known progressive cocoon boiling machine. As the endless chain stored in the cocoon container advances, it passes continuously through the immersion tank 6, the catalytic chamber 7, and the permeation tank 8, is treated at each part and is affected by steam, and enters the cocoon layer as described above. The water is absorbed into the steaming chamber 9 and the adjustment tank 10.

蒸煮室9は予め減圧装置12により所要負圧を維持して
おり、又調整槽10はそれに対応して所定の沸点で煮沸
している。
The steaming chamber 9 is maintained at a required negative pressure in advance by a pressure reducing device 12, and the regulating tank 10 is correspondingly boiled at a predetermined boiling point.

繭容器に収容された繭は蒸煮室9で飽和蒸気に接触して
繭腔4内の空気が蒸気に置き換えられた後、直ちに所定
湯混の調整槽10内へ入り、次いで大気圧に近ずくに従
って徐々に温度を降下して繭腔内に湯水を浸透させ、大
気圧域に出て玉樋14に収容され、煮繭が完了する。
The cocoons housed in the cocoon container come into contact with saturated steam in the steaming chamber 9, and the air in the cocoon cavity 4 is replaced with steam, and then immediately enters the adjustment tank 10 containing a predetermined hot water mixture, and then approaches atmospheric pressure. Accordingly, the temperature is gradually lowered to allow hot water to penetrate into the cocoon cavity, and the cocoon comes out to the atmospheric pressure region and is accommodated in the tamahi 14, completing the boiling of the cocoon.

本発明は上記実施例の如く行うもので、処理工程中圧力
変化を生ずる過程が総べて湯水中であるので、煮繭斑の
起生がなく、又負圧状態の飽和蒸気中で蒸煮を行うので
、繭に蒸気を十分作用させることができる。
The present invention is carried out in the same way as in the above embodiments, and since the entire process that causes pressure changes during the treatment process is done in hot water, there is no occurrence of boiling spots on the cocoons, and steaming is carried out in saturated steam under negative pressure. This allows the cocoons to be sufficiently exposed to steam.

又調整槽の沸点を所定の負圧に応じて制御できる様にし
ているから、過剰の蒸気が供給されたとしても所定温度
、例えば96℃を維持することが可能であり、使用原繭
に対応して100℃以下の温度で処理することを可能と
し、又飽和蒸気室である蒸煮室から直ちに煮沸湯へ導入
するから略々100%近く繭腔中に吸水させることが出
来、浮き繭を完全になくすことができる。
In addition, since the boiling point of the adjustment tank can be controlled according to a predetermined negative pressure, it is possible to maintain a predetermined temperature, for example, 96°C, even if excess steam is supplied, which corresponds to the original cocoon used. This makes it possible to process the water at a temperature below 100°C, and since the water is immediately introduced into the boiling water from the steaming chamber, which is a saturated steam chamber, almost 100% of the water can be absorbed into the cocoon cavity, and the floating cocoons can be completely removed. can be lost.

更に調整槽が傾斜しているため温度勾配がとりやすくそ
のため繭に接触する温度を自由にコントロールすること
も可能である。
Furthermore, since the adjustment tank is tilted, it is easy to create a temperature gradient, which makes it possible to freely control the temperature at which the cocoon comes into contact.

尚処理温度及び時間を適切に設定することにより、本実
施例の前処理工程を削除してもさしつかえない。
Note that the pretreatment step of this example may be omitted by appropriately setting the treatment temperature and time.

この場合は蒸煮室に隣接する前記水槽が前処理槽となる
In this case, the water tank adjacent to the steaming chamber serves as the pretreatment tank.

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

第1図は繭の縦断面を示す説明図、第2図は本発明に用
いる装置の一例を示す要部だけの縦断面図である。 1・・・・・・繭層、2・・・・・・粗の部分、3・・
・・・・密の部分、4・・・・・・繭腔、5・・・・・
・無端鎖、6・・・・・・浸漬槽、7・・・・・・触蒸
室、8・・・・・・滲透槽、9・・・・・・蒸煮室、1
0・・・・・・調整槽、11・・・・・・供気口、12
・・・・・・減圧装置、13・・・・・・蒸気供給バル
ブ、14・・・・・・玉樋。
FIG. 1 is an explanatory view showing a longitudinal section of a cocoon, and FIG. 2 is a longitudinal sectional view of only essential parts showing an example of the apparatus used in the present invention. 1...cocoon layer, 2...coarse part, 3...
...Dense part, 4...Cocoon cavity, 5...
・Endless chain, 6... Immersion tank, 7... Touching chamber, 8... Permeation tank, 9... Steaming chamber, 1
0...Adjustment tank, 11...Air supply port, 12
...... Pressure reduction device, 13... Steam supply valve, 14... Ball gutter.

Claims (1)

【特許請求の範囲】[Claims] 1 少くとも前処理工程、蒸煮工程、調整工程を順次経
由せしめる連続煮繭方法であって、前処理工程により浸
漬及び滲透処理を受けた繭粒を、飽和蒸気が充満し且つ
大気圧未満の所定負圧に保たれた蒸煮室に通し、引き続
いて前記蒸煮室に密接する調整槽上部の100℃未満の
煮繭水に没入させ、繭粒移送方向に向って順次圧力を高
め大気圧に達する前記煮繭水を経由せしめて煮繭するこ
とを特徴とする煮繭方法。
1 A continuous cocoon boiling method that sequentially passes through at least a pretreatment step, a steaming step, and a conditioning step, in which the cocoon grains that have been soaked and permeated in the pretreatment step are heated to a predetermined temperature filled with saturated steam and at a pressure below atmospheric pressure. The cocoons are passed through a steaming chamber maintained at negative pressure, and then immersed in boiled water of less than 100°C in the upper part of a regulating tank that is in close contact with the steaming chamber, and the pressure is gradually increased in the direction of cocoon grain transfer until it reaches atmospheric pressure. A cocoon boiling method characterized by boiling cocoons through boiling cocoon water.
JP8641081A 1981-06-04 1981-06-04 Boiled cocoon method Expired JPS5812363B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8641081A JPS5812363B2 (en) 1981-06-04 1981-06-04 Boiled cocoon method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8641081A JPS5812363B2 (en) 1981-06-04 1981-06-04 Boiled cocoon method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP49064322A Division JPS5810483B2 (en) 1974-06-05 1974-06-05 Shakenki

Publications (2)

Publication Number Publication Date
JPS57191314A JPS57191314A (en) 1982-11-25
JPS5812363B2 true JPS5812363B2 (en) 1983-03-08

Family

ID=13886090

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8641081A Expired JPS5812363B2 (en) 1981-06-04 1981-06-04 Boiled cocoon method

Country Status (1)

Country Link
JP (1) JPS5812363B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104313700A (en) * 2014-11-19 2015-01-28 兴化市丝尚春丝制品厂 Fresh cocoon cooking device

Also Published As

Publication number Publication date
JPS57191314A (en) 1982-11-25

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