JP4560635B2 - Sericin separation and recovery equipment - Google Patents

Sericin separation and recovery equipment Download PDF

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Publication number
JP4560635B2
JP4560635B2 JP2000119769A JP2000119769A JP4560635B2 JP 4560635 B2 JP4560635 B2 JP 4560635B2 JP 2000119769 A JP2000119769 A JP 2000119769A JP 2000119769 A JP2000119769 A JP 2000119769A JP 4560635 B2 JP4560635 B2 JP 4560635B2
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Prior art keywords
jacket
scouring
sericin
freezing
vertical pipe
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JP2001302693A (en
Inventor
正夫 山崎
哲郎 片山
裕美 田中
功 嶋津
文男 梅田
修 永砂
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ながすな繭株式会社
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Description

【0001】
【発明の属する技術分野】
絹繊維から、高分子量のセリシンを収率よく得るための装置に関する。
【0002】
【従来の技術】
絹セリシンを有効使用しようとする試みは種々なされており、特に特開平11−131318号公報に開示される如く、絹繊維を高温水で高温高圧処理して得た精練液を、凍結・解凍することにより、高分子量のセリシンを分離回収することができることも知られている。しかし、この方法を効率よく実施するためには、その凍結・解凍の工程を慎重に制御する必要があり、従来の凍結装置等によっては、工業的に実施することはできなかった。
【0003】
【発明が解決しようとする課題】
絹繊維を高温水で高温高圧処理して得た精練液すなわちセリシン水溶液を、凍結・解凍して、高分子量のセリシンを製造するという方法で、分子量が10万以上という高分子量のセリシンを安定して得るには、セリシン水溶液の凍結を約8時間以上かけてゆっくり実施し、更に、その後−10℃以下に十分冷却して凍結を完了するのがよいことがわかっている。そこで、本発明では、セリシン水溶液を0℃近辺で8時間以上かけて、均一に穏やかに、凍結することができ、しかも凍結前後の工程も、非常に作業性良く、無駄なく実施できる装置を提供することを課題とする。
【0004】
【課題を解決するための手段】
本発明では、保温断熱性を有するジャケット内に、下端に絹繊維の精練液導入口を有し、上面に多数本の立管を設けたマニホールドを設置し、この立管内に導入、貯留された精練液を、前記ジャケット内で凍結・解凍するようにしたことによって、上記課題を解決した。なお、精練液の凍結温度は空冷により、温度制御可能とした。
【0005】
即ち、本発明では、例えばセリシンを0.2〜2.5%程度含有する精練液を、立管内に分割貯留し、冷凍コンデンサー等を使用した空冷で、凍結できるため、時間をかけて(例えば、液温0℃近辺で8時間以上かけて)徐々に凍結し、その後、液温を約−10℃以下に冷却し凍結を完了するという方法を、非常に効率よく、均一に実施できる。また、凍結した精練液を、ジャケット内で、そのまま効率よく解凍することも可能となる。
【0006】
なお、立管は、精練液の凍結を均一に徐々に凍結するという目的から、直径500mm以下とされるのがよいが、直径50〜300mm、特に70〜200mm程度とするのが好ましい。
【0007】
ジャケット内で、精練液を貯留し、凍結・解凍するための立管群は、仕切板で囲まれた状態で存在させるのが好ましく、仕切板の下端は、マニホールドの上面に対して一定間隔を開けた状態で位置するようにするのがよい。この場合、冷凍コンデンサー等により送られる冷気は、仕切板内部で立管の周囲を上方から下方に流れ、仕切板の下端から、仕切板とジャケット内壁の間に出るという流路で、ジャケット内を循環するようになる。
【0008】
なお、立管内の精練液を0℃近辺で長時間かけて凍結するように、ジャケット内の冷気は、0℃〜−6℃程度に安定して温度制御される必要があるため、その温度制御には、通常冷凍コンデンサーを使用するのが好ましく、また冷凍コンデンサーと暖房用コンデンサーを併用してもよい。
【0009】
立管内で凍結された精練液は、そのままの状態で、解凍するものであり、この解凍は、暖房用コンデンサーによる温風で実施してもよいが、温水を用いて実施するのが好ましい。そのため、ジャケットの下方に、温水導入口を設けるのがよく、ジャケット内に導入された温水は、立管を越えない一定高さで自動的に水位が調節されるように液面センサーで制御されるのがよい。
【0010】
【発明の実施の形態】
次に、本発明を図面に示す一例に従って、更に詳細に説明する。
図1の装置は、保温断熱性を有するジャケット1内に、下端に絹繊維の精練液導入口2を有し、上面に多数本の立管3を設けたマニホールド4が設置されたものであり、立管3の上方には、冷凍コンデンサー5が設置されており、ファン7により、冷凍コンデンサー5からの冷気が下方に送られ、立管3内に導入、貯留された精練液を、この冷気により凍結するようになっている。
【0011】
なお、この例では、ジャケット内の立管3の直径を80mmとし、立管3は仕切板8で囲まれた状態で、前記ジャケット内に存在しており、仕切板8の下端はマニホールド4の上面に対して一定間隔を開けた状態で位置しており、冷凍コンデンサー5からの冷気が、仕切板8内部、立管3の周囲を均等に冷却しながら下降し、仕切板8の下端とマニホールド4の上面の間から、ジャケット1と仕切板8の間に出て、そこを上昇し、ジャケット1内を循環するようになっている。
【0012】
冷凍コンデンサー5は、冷気を0〜−6℃程度に保ち、立管3内の精練液を0℃近辺で長時間をかけて凍結するように、制御されるが、必要に応じて、冷凍コンデンサー5の上方に設けた暖房用コンデンサー6を併用して、この温度制御を実施できるようになっている。
【0013】
立管3内の精練液は0℃近辺で長時間をかけて凍結した後、−10℃以下に冷却して凍結を完了し、その結果、分子量が10万以上という高分子量のセリシンを析出可能とする。このセリシンは、立管3内で精練液を解凍して、解凍液を取り出し、遠心分離機で、分離するが、解凍液の取り出しは、マニホールド4の精練液導入口2を通して実施するようになっている。
【0014】
この装置では、凍結した精練液の解凍を効率よく実施するため、50℃前後の温水を利用するものであり、ジャケット1の底面に温水導入口9が設けられている。なお、導入された温水の高さは、ジャケット1内で立管3の口部近くに保たれるように、液面センサー10aにより位置制御されている。通常、50℃前後の温水をジャケット内に3度程度入れ換えることにり、凍結した精練液に流動性を持たせ、解凍液として、精練液導入口2から、遠心分離機側に取り出すようになっている。
【0015】
更に、この装置は、精練液の導入量を制御する(立管3の口部近くに液面を制御する)ために、液面センサー10bを設けているが、通常は、立管3等の容積に適合する量の精練液を準備して、一回毎に、それを導入処理するのがよい。これは、凍結・解凍を、立管3内で完全にシールド状態で実施するためである。
【0016】
解凍液に含まれる高分子量のセリシンは、立管3やマニホールド4の壁面に付着して、完全に流出し難いので、この装置では、立管3の上部及び/又はマニホールド4の側面に、洗浄水用のノズル11を取り付け、高圧水を噴霧させて残留するセリシンを回収できるようになっている。
【0017】
次に、この装置の使用例を示す。
絹織物3反を、60℃×30分の精練前処理後、120℃×30分の無薬剤高温精練して、セリシン含有率0.3%の精練液150リットルを得た。
図1の装置を、予め冷凍運転し、ジャケット内の温度を0〜5℃程度に下げた後、上記精練液150リットルを精練液導入口2から立管3内に導入した。その後、冷凍コンプレッサーの運転、休止を時間管理して、図2の如く、立管3内の液温を、+5℃から−2℃迄、約10時間かけて、徐々に冷凍し、その後、−10℃以下に凍結した。なお、立管3の周囲の気温は、最初の8時間程度は−5℃〜−7℃程度に保たれ、その後−15℃迄冷却されるように、温度制御されている。
【0018】
凍結が終了すると、ジャケット1の温水導入口9から50℃の温水を導入し、立管3内の凍結した精練液を解凍する。温水は、液面センサー10aで制御し、立管3の口部近く迄導入し、一定時間保持し、排出するという工程を3度繰り返し、立管3内の精練液を解凍し、精練液導入口2から遠心分離機にポンプで圧送した後、立管内及びマニホールドに高圧水を、ノ ズル11を通して、噴霧させて残留するセリシンを回収した。
【0019】
このようにして得た解凍液を遠心分離機で脱水し、乾燥した結果、分子量129,000のセリシンを282g(回収率63.5%)を得ることができた。
【0020】
【発明の効果】
本発明の装置では、絹繊維(生糸等)から、操作性よく、高分子量のセリシンを製造できる。精練液の凍結温度の制御を空冷で実施できるため、凍結時間を容易に一定に保つことが可能となり、安定して、再現性よく、高分子量のセリシンの回収が可能となる。また、精練液の凍結・解凍処理を同一装置内で、効率よく実施できるという効果もある。
【図面の簡単な説明】
【図1】図1は、本発明の装置の一例を示す説明図である。
【図2】図2は、本発明の装置の一使用例における、温度変化を示すグラフである。
【符号の説明】
1 ジャケット
2 精練液導入口
3 立管
4 マニホールド
5 冷凍コンデンサー
6 暖房用コンデンサー
7 ファン
8 仕切板
9 温水導入口
10a、10b 液面センサー
11 ノ ズル
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for obtaining high-molecular-weight sericin from silk fibers with high yield.
[0002]
[Prior art]
Various attempts have been made to effectively use silk sericin. In particular, as disclosed in JP-A-11-131318, a scouring solution obtained by high-temperature and high-pressure treatment of silk fibers with high-temperature water is frozen and thawed. Thus, it is also known that high molecular weight sericin can be separated and recovered. However, in order to carry out this method efficiently, it is necessary to carefully control the freezing and thawing process, and it has not been possible to carry out industrially with a conventional freezing apparatus or the like.
[0003]
[Problems to be solved by the invention]
A high-molecular-weight sericin having a molecular weight of 100,000 or more is stabilized by freezing and thawing a scouring solution obtained by treating silk fiber with high-temperature and high-pressure water at high temperature and pressure, that is, a sericin aqueous solution. It has been found that the sericin aqueous solution should be slowly frozen for about 8 hours or longer, and then cooled to -10 ° C. or lower to complete the freezing. Therefore, the present invention provides an apparatus that can freeze a sericin aqueous solution uniformly and gently over 8 hours at around 0 ° C., and that can perform processes before and after freezing with very good workability and without waste. The task is to do.
[0004]
[Means for Solving the Problems]
In the present invention, a jacket having a silk fiber scouring liquid inlet at the lower end and a manifold having a large number of vertical pipes on the upper surface are installed in the jacket having heat insulation and heat insulation properties, and the manifold is introduced and stored in this vertical pipe. The above problem was solved by freezing and thawing the scouring liquid in the jacket. The freezing temperature of the scouring solution can be controlled by air cooling.
[0005]
That is, in the present invention, for example, a scouring solution containing about 0.2 to 2.5% of sericin can be stored in divided tubes in the vertical pipe and frozen by air cooling using a refrigeration condenser or the like. The method of gradually freezing at a liquid temperature of about 0 ° C. over 8 hours and then cooling the liquid temperature to about −10 ° C. or lower to complete the freezing can be carried out very efficiently and uniformly. In addition, the frozen scouring solution can be efficiently thawed as it is in the jacket.
[0006]
The vertical tube is preferably set to have a diameter of 500 mm or less for the purpose of uniformly and gradually freezing the scouring solution, but preferably has a diameter of 50 to 300 mm, particularly about 70 to 200 mm.
[0007]
The standing tube group for storing, freezing and thawing the scouring liquid in the jacket is preferably present in a state surrounded by the partition plate, and the lower end of the partition plate is spaced apart from the upper surface of the manifold by a certain distance. It should be positioned in an open state. In this case, the cold air sent by the refrigeration condenser or the like flows in the inside of the jacket through a flow path that flows from the upper side to the lower side of the vertical pipe inside the partition plate and exits between the lower end of the partition plate and the inner wall of the jacket. It comes to circulate.
[0008]
Note that the temperature of the cool air in the jacket needs to be stably controlled at about 0 ° C. to −6 ° C. so that the scouring liquid in the vertical tube is frozen at around 0 ° C. for a long time. In general, a refrigeration condenser is preferably used, and a refrigeration condenser and a heating condenser may be used in combination.
[0009]
The scouring solution frozen in the vertical pipe is thawed as it is, and this thawing may be carried out with warm air using a heating condenser, but is preferably carried out using hot water. Therefore, it is recommended to provide a hot water inlet at the bottom of the jacket, and the hot water introduced into the jacket is controlled by a liquid level sensor so that the water level is automatically adjusted at a certain height not exceeding the vertical pipe. It is better.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Next, the present invention will be described in more detail with reference to an example shown in the drawings.
The apparatus shown in FIG. 1 has a jacket 1 having heat insulation and heat insulation, and a manifold 4 having a silk fiber scouring fluid inlet 2 at its lower end and a plurality of vertical tubes 3 on its upper surface. The refrigeration condenser 5 is installed above the vertical pipe 3, and the cool air from the refrigeration condenser 5 is sent downward by the fan 7, and the scouring liquid introduced and stored in the vertical pipe 3 is supplied with this cold air. To freeze.
[0011]
In this example, the diameter of the vertical pipe 3 in the jacket is 80 mm, the vertical pipe 3 is surrounded by the partition plate 8 and exists in the jacket, and the lower end of the partition plate 8 is the bottom of the manifold 4. It is located in a state where it is spaced apart from the upper surface, and the cold air from the refrigeration condenser 5 descends while uniformly cooling the inside of the partition plate 8 and the periphery of the vertical pipe 3, and the lower end of the partition plate 8 and the manifold From between the upper surface of 4, it comes out between the jacket 1 and the partition plate 8, rises there, and circulates in the jacket 1.
[0012]
The refrigeration condenser 5 is controlled so that the cold air is kept at about 0 to -6 ° C. and the scouring liquid in the vertical tube 3 is frozen at a temperature around 0 ° C. over a long period of time. This temperature control can be carried out by using together with a heating condenser 6 provided above 5.
[0013]
The scouring liquid in the vertical pipe 3 is frozen at around 0 ° C. for a long time, and then cooled to −10 ° C. or lower to complete the freezing. As a result, high molecular weight sericin having a molecular weight of 100,000 or higher can be precipitated. And This sericin thaws the scouring solution in the vertical tube 3, removes the thawing solution, and separates it with a centrifuge, and the thawing solution is taken out through the scouring fluid inlet 2 of the manifold 4. ing.
[0014]
In this apparatus, hot water at around 50 ° C. is used to efficiently thaw the frozen scouring liquid, and a hot water inlet 9 is provided on the bottom surface of the jacket 1. The height of the introduced hot water is controlled by the liquid level sensor 10a so as to be maintained near the mouth of the vertical pipe 3 in the jacket 1. Usually, hot water at around 50 ° C. is exchanged about 3 times in the jacket, the frozen scouring liquid is made fluid, and it is taken out from the scouring liquid inlet 2 to the centrifuge as a thawing liquid. ing.
[0015]
Furthermore, this apparatus is provided with a liquid level sensor 10b for controlling the amount of scouring liquid introduced (controlling the liquid level near the mouth of the vertical pipe 3). It is preferable to prepare an amount of scouring liquid suitable for the volume, and to introduce it every time. This is because freezing and thawing are performed in a completely shielded state in the vertical pipe 3.
[0016]
Since the high molecular weight sericin contained in the thawing solution adheres to the wall surfaces of the vertical pipe 3 and the manifold 4 and hardly flows out completely, in this apparatus, the upper part of the vertical pipe 3 and / or the side surface of the manifold 4 is washed. A nozzle 11 for water is attached, and high pressure water is sprayed to recover the remaining sericin.
[0017]
Next, the usage example of this apparatus is shown.
The silk fabric 3 was scoured at 60 ° C. for 30 minutes and then scoured at 120 ° C. for 30 minutes without chemicals to obtain 150 liters of a scouring solution having a sericin content of 0.3%.
The apparatus shown in FIG. 1 was refrigerated in advance, the temperature in the jacket was lowered to about 0 to 5 ° C., and 150 liters of the scouring liquid was introduced into the vertical pipe 3 from the scouring liquid inlet 2. Thereafter, the operation and stop of the refrigeration compressor are time-controlled, and the liquid temperature in the vertical pipe 3 is gradually frozen from + 5 ° C. to −2 ° C. over about 10 hours as shown in FIG. Frozen below 10 ° C. The temperature around the vertical pipe 3 is controlled to be maintained at about -5 ° C to -7 ° C for the first 8 hours and then cooled to -15 ° C.
[0018]
When freezing is completed, hot water at 50 ° C. is introduced from the hot water inlet 9 of the jacket 1, and the frozen scouring liquid in the vertical tube 3 is thawed. The hot water is controlled by the liquid level sensor 10a, introduced to the vicinity of the mouth of the vertical pipe 3, held for a certain period of time, and discharged three times to thaw the scouring liquid in the vertical pipe 3 and introduce the scouring liquid. After pumping from the port 2 to the centrifuge, high pressure water was sprayed through the nozzle 11 in the vertical pipe and the manifold, and the remaining sericin was recovered.
[0019]
The thawed solution thus obtained was dehydrated with a centrifuge and dried. As a result, 282 g of sericin having a molecular weight of 129,000 (recovery rate: 63.5%) could be obtained.
[0020]
【The invention's effect】
In the apparatus of the present invention, high molecular weight sericin can be produced from silk fibers (raw silk, etc.) with good operability. Since the freezing temperature of the scouring solution can be controlled by air cooling, the freezing time can be easily maintained constant, and high-molecular weight sericin can be recovered stably and with good reproducibility. In addition, there is an effect that the scouring solution can be efficiently frozen and thawed in the same apparatus.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing an example of an apparatus according to the present invention.
FIG. 2 is a graph showing temperature changes in an example of use of the apparatus of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Jacket 2 Scouring liquid inlet 3 Stand pipe 4 Manifold 5 Refrigeration condenser 6 Heating condenser 7 Fan 8 Partition plate 9 Hot water inlet 10a, 10b Liquid level sensor 11 Nozzle

Claims (4)

保温断熱性を有するジャケット内に、下端に絹繊維の精練液導入口を有し、上面に多数本の立管を設けたマニホールドが設置されており、この立管内に導入、貯留された精練液を、前記ジャケット内で凍結・解凍するものであって、精練液の凍結温度が空冷により、温度制御されるようになっていることを特徴とするセリシンを分離回収するための装置。A jacket with a silk fiber scouring fluid inlet at the lower end and a large number of vertical pipes on the upper surface is installed in a jacket having heat insulation and heat insulation properties. For freezing and thawing the sericin in the jacket, wherein the freezing temperature of the scouring solution is controlled by air cooling. 前記立管群が、仕切板で囲まれた状態で、前記ジャケット内に存在すること、及び前記仕切板の下端がマニホールドの上面に対して一定間隔を開けた状態で位置することを特徴とする請求項1の装置。The standing pipe group is present in the jacket in a state surrounded by a partition plate, and the lower end of the partition plate is positioned in a state of being spaced apart from the upper surface of the manifold. The apparatus of claim 1. 前記凍結温度が冷凍コンデンサー又は冷凍コンデンサーと暖房用コンデンサーの併用により、温度制御されるようになっていることを特徴とする請求項1又は2の装置。The apparatus according to claim 1 or 2, wherein the freezing temperature is temperature-controlled by a refrigeration condenser or a combination of a refrigeration condenser and a heating condenser. 前記ジャケットの下方に、立管内で凍結したセリシン水溶液を解凍するための温水を導入する、温水導入口が設けられていることを特徴とする請求項1〜3いずれか1項の装置。The apparatus according to any one of claims 1 to 3, wherein a hot water inlet for introducing hot water for thawing the sericin aqueous solution frozen in the vertical pipe is provided below the jacket.
JP2000119769A 2000-04-20 2000-04-20 Sericin separation and recovery equipment Expired - Lifetime JP4560635B2 (en)

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CN103993363B (en) * 2014-06-10 2015-12-09 横县桂华茧丝绸有限责任公司 Solar energy boils continuous equipment
CN104947202A (en) * 2015-06-16 2015-09-30 苏州维度丝绸有限公司 Real silk soaking device
CN104947203B (en) * 2015-06-16 2017-07-21 安溪县桃舟乡同盛茶叶专业合作社 A kind of silk soaks cylinder
CN104947204B (en) * 2015-06-16 2017-01-18 谢彩红 Real silk soaking trolley
CN105642658B (en) * 2016-03-20 2018-05-29 广西百姓人家家纺有限公司 Silk floss filature silk silk floss slag biology corruption processing method and equipment
CN113227469B (en) * 2018-08-03 2023-05-16 塔夫茨大学信托人 Automated process for extraction of silk fibroin
CN114622289B (en) * 2022-03-31 2023-09-22 河南民兴生物科技股份有限公司 Tussah silk degumming device and tussah silk degumming method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11131318A (en) * 1997-10-30 1999-05-18 Kyoto Prefecture Method for separating and recovering sericin

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