JP2609826B2 - Vertical package dyeing processing equipment - Google Patents
Vertical package dyeing processing equipmentInfo
- Publication number
- JP2609826B2 JP2609826B2 JP28935494A JP28935494A JP2609826B2 JP 2609826 B2 JP2609826 B2 JP 2609826B2 JP 28935494 A JP28935494 A JP 28935494A JP 28935494 A JP28935494 A JP 28935494A JP 2609826 B2 JP2609826 B2 JP 2609826B2
- Authority
- JP
- Japan
- Prior art keywords
- processing
- carrier
- blower
- liquid
- tank
- 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
Landscapes
- Treatment Of Fiber Materials (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は気液混合流体により低浴
比処理を行なう竪型パッケージ染色処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vertical package dyeing apparatus for performing a low bath ratio treatment with a gas-liquid mixed fluid.
【0002】[0002]
【0003】旧来の竪型パッケージ染色処理装置は、図
3に示すように、キャリア3の各スピンドル6に積重さ
れたチーズ等のパッケージ繊維製品Pが、処理槽2内で
完全に処理液Lに浸漬するように処理液面Sを保持し、
チーズの内側→外側、及び外側→内側へと循環処理液の
切換えにより染色等の処理を行なっていた。従って浴比
は1:20以上となって染料・薬品は勿論のこと、処理
液の加熱/冷却に伴なうエネルギーの消費は膨大なもの
であった。As shown in FIG. 3, in a conventional vertical package dyeing apparatus, a package fiber product P such as cheese stacked on each spindle 6 of a carrier 3 is completely treated with a processing solution L in a processing tank 2. Holding the processing liquid surface S so as to be immersed in
Processing such as dyeing has been performed by switching the circulating treatment liquid from inside to outside and outside to inside of the cheese. Therefore, the bath ratio was 1:20 or more, and the consumption of energy accompanying heating / cooling of the processing solution as well as dyes and chemicals was enormous.
【0004】そこで石油ショックを機に省エネ化が進め
られてきたが、最近の低浴比処理方法は、処理槽2内
の処理液面Sを下げたり、繊維チーズの巻密度や容量
を増大させるなどの方法で対応していたが、1:6が低
浴比化の限界であった。Therefore, energy saving has been promoted in response to the oil shock. However, recent low bath ratio treatment methods lower the treatment liquid level S in the treatment tank 2 or increase the winding density and capacity of the fiber cheese. However, 1: 6 was the limit of lowering the bath ratio.
【0005】本発明の目的は、パッケージ繊維製品の処
理において一層の低浴比化を推進することにある。An object of the present invention is to promote a further lower bath ratio in the treatment of packaged textile products.
【0006】[0006]
【課題を解決するための手段】前記課題を解決するため
本発明の竪型パッケージ染色処理装置は、チーズ等のパ
ッケージ繊維製品を積重したスピンドルを多数並立設し
たキャリアを装填してなる染色処理槽と、前記キャリア
の内部空間と前記キャリアの外部空間である処理槽と
を、ブロワを有する気流循環路で連通すると共に、前記
パッケージ繊維製品を貫流した後の気流から分離された
処理液を貯溜する液溜からポンプ及び熱交換器を介して
前記ブロワの吐出側気流循環路に挿入した噴霧ノズルに
至る処理液循環路を形成した。ブロアから吐出された気
流を、キャリアの内部空間に導入する形式(イン・アウ
ト形式)と、キャリアの外部空間である処理槽内に導入
する形式(アウト・イン形式)が可能であり、パッケー
ジ繊維製品の種類や処理内容等によって2つの形式を使
い分ける。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, a vertical package dyeing apparatus of the present invention is a dyeing processing method in which a carrier having a large number of spindles stacked with packaged fiber products such as cheese is mounted in parallel. A tank, an inner space of the carrier, and a processing tank that is an outer space of the carrier are communicated by an airflow circuit having a blower, and a processing liquid separated from an airflow after flowing through the package fiber product is stored. A treatment liquid circulation path was formed from the liquid reservoir to the spray nozzle inserted into the discharge-side airflow circulation path of the blower via a pump and a heat exchanger. The airflow discharged from the blower can be introduced into the internal space of the carrier (in-out type) or into the processing tank that is the external space of the carrier (out-in type). The two types are properly used depending on the type of the product, the processing content, and the like.
【0007】[0007]
【作用】ブロアから吐出された気流をキャリアの内部空
間に導入する形式では、気流が気流循環路を通ってキャ
リアの内部空間に供給される途中で噴霧ノズルから霧状
処理液が供給されて、気液混合流体が生成される。この
気液混合流体は、キャリアのスピンドルに積重されたパ
ッケージ繊維製品を内側から外側へ半径方向に還流した
後、気流は吸込側気流循環路からブロワに還流され、処
理液は液溜に接続された処理液循環路からポンプ及び熱
交換器を介して前記噴霧ノズルに循環供給される。In the type in which the air flow discharged from the blower is introduced into the internal space of the carrier, the atomizing processing liquid is supplied from the spray nozzle while the air flow is supplied to the internal space of the carrier through the air flow circulation path. A gas-liquid mixed fluid is generated. After the gas-liquid mixed fluid returns radially from the inside to the outside of the package fiber product stacked on the spindle of the carrier, the airflow is returned to the blower from the suction-side airflow circuit, and the processing liquid is connected to the liquid reservoir. The circulated processing liquid is circulated and supplied to the spray nozzle via a pump and a heat exchanger.
【0008】またブロアから吐出された気流をキャリア
の外部空間である処理槽内に導入する形式では、気流が
気流循環路を通って処理槽内に導入される途中で噴霧ノ
ズルから霧状処理液が供給されて、気液混合流体が生成
される。この気液混合流体は、キャリアのスピンドルに
積重されたパッケージ繊維製品を外側から内側へ半径方
向に還流した後、気流はスピンドル内を流下して吸込側
気流循環路からブロワに還流され、処理液は液溜に接続
された処理液循環路からポンプ及び熱交換器を介して前
記噴霧ノズルに循環供給される。In the type in which the air flow discharged from the blower is introduced into the processing tank, which is the external space of the carrier, the atomizing processing liquid is sprayed from the spray nozzle while the air flow is introduced into the processing tank through the air flow circulation path. Is supplied to generate a gas-liquid mixed fluid. The gas-liquid mixed fluid radially returns the package fiber product stacked on the spindle of the carrier from the outside to the inside in the radial direction.After that, the airflow flows down the spindle and is returned to the blower from the suction-side airflow circulation path to be processed. The liquid is circulated and supplied from the processing liquid circulation path connected to the liquid reservoir to the spray nozzle via a pump and a heat exchanger.
【0009】[0009]
【実施例】以下に本発明の実施例を図に基づいて説明す
る。図1はイン・アウト形式の竪型パッケージ染色処理
装置1であって、竪型円筒状の密閉形処理槽2と、この
処理槽2内部に搬出入可能に装填されるキャリア3と、
処理槽2の外側に配設されたブロア4及び投入槽5とを
有する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows an in-out type vertical package dyeing and processing apparatus 1, which is a vertical cylindrical hermetically sealed processing tank 2, and a carrier 3 that is loaded into and out of the processing tank 2,
It has a blower 4 and a charging tank 5 disposed outside the processing tank 2.
【0010】処理槽2の上部には開閉自在な蓋2aが被
冠し、底部は緩慢な漏斗状をなし、この底部中央下方に
処理液溜2bが形成されている。キャリア3はチーズ等
のパッケージ繊維製品Pを積重したスピンドル6を多数
並立設してなり、キャリア3の下部は中空な基部3aと
されている。この基部3aの内部と各スピンドル6の内
部は連通しており、基部3aが各スピンドル6へ気液混
合流体を分配するヘッダとなっている。この基部3aの
下面中心部には気液混合流体を導入するための入口開口
部7が形成されている。また処理槽2の下部側壁には、
配管8が水平方向に貫通配設され、この配管8の内端は
処理槽2中心部まで延出した後、垂直方向上方に屈曲さ
れ気液混合流体の出口開口部8aとして上向きに開口し
ている。そしてこの出口開口部8aにキャリア3の基部
3aの入口開口部7が着脱自在に接続されている。An openable and closable lid 2a covers the upper portion of the processing tank 2, the bottom has a slow funnel shape, and a processing liquid reservoir 2b is formed below the center of the bottom. The carrier 3 is composed of a number of spindles 6 stacked with package fiber products P such as cheese, and a lower portion of the carrier 3 is a hollow base 3a. The inside of the base 3a communicates with the inside of each spindle 6, and the base 3a serves as a header for distributing the gas-liquid mixed fluid to each spindle 6. An inlet opening 7 for introducing a gas-liquid mixed fluid is formed at the center of the lower surface of the base 3a. Also, on the lower side wall of the processing tank 2,
A pipe 8 is provided to penetrate in the horizontal direction. The inner end of the pipe 8 extends to the center of the processing tank 2, and then is bent upward in the vertical direction to open upward as an outlet opening 8 a for the gas-liquid mixed fluid. I have. The inlet opening 7 of the base 3a of the carrier 3 is detachably connected to the outlet opening 8a.
【0011】処理槽2の外壁面には水平方向外側に延出
したブラケット9が固定され、このブラケット9上にモ
ータ10で駆動されるブロワ4が設置されている。ブロ
ワ4の吸込口4aは、処理槽2の高さ方向ほぼ中間位置
にて処理槽2外壁面に突設された出口開口部2cに接続
されている。またブロワ4の吐出口4bは、処理槽2外
に延びた配管8の垂直端部8bに接続されている。そし
て、ブロワ4→吐出口4b→配管8→キャリア3の基部
3a→各スピンドル6→処理槽2の出口開口部2c→吸
込口4a→ブロワ4の経路の気流循環路Aが形成されて
いる。A bracket 9 extending outward in the horizontal direction is fixed to the outer wall surface of the processing tank 2, and a blower 4 driven by a motor 10 is installed on the bracket 9. The suction port 4a of the blower 4 is connected to an outlet opening 2c protruding from the outer wall surface of the processing tank 2 at a substantially intermediate position in the height direction of the processing tank 2. The discharge port 4b of the blower 4 is connected to a vertical end 8b of a pipe 8 extending outside the processing tank 2. Then, an air flow circulation path A is formed from the blower 4 → the discharge port 4b → the pipe 8 → the base 3a of the carrier 3 → the respective spindles 6 → the outlet opening 2c of the processing tank 2 → the suction port 4a → the blower 4.
【0012】配管8の途中のエルボ部8cには噴霧ノズ
ル11が下流に向けて挿入されている。この噴霧ノズル
11は処理液循環路Bによって処理液溜2bに接続され
ている。処理液循環路Bには処理液溜2b側から順に、
循環ポンプ13と熱交換器14と調整バルブ15が配設
されている。A spray nozzle 11 is inserted downstream of the elbow 8c in the middle of the pipe 8. The spray nozzle 11 is connected to the processing liquid reservoir 2b by a processing liquid circulation path B. In the processing liquid circulation path B, in order from the processing liquid reservoir 2b side,
A circulation pump 13, a heat exchanger 14, and a regulating valve 15 are provided.
【0013】投入槽5は、染料や助剤を溶解、攪拌して
処理槽2へ導入するためのものである。投入槽5の内部
にはスチームパイプ16と、モータ17で回転されるミ
キサ18が配設されている。投入槽5は供給路19によ
って処理液溜2bに接続され、この供給路19にポンプ
20、チャッキ弁21及び調整弁22が配設されてい
る。The charging tank 5 is for dissolving and stirring the dyes and auxiliaries and introducing them into the processing tank 2. Inside the charging tank 5, a steam pipe 16 and a mixer 18 rotated by a motor 17 are provided. The charging tank 5 is connected to the processing liquid reservoir 2 b by a supply path 19, and a pump 20, a check valve 21, and an adjustment valve 22 are provided in the supply path 19.
【0014】処理装置1によるパッケージ繊維製品Pの
処理は次のように行なわれる。まず処理槽2の蓋2aを
開けてキャリア3を処理槽2内に装填した後、蓋2aを
密閉する。次にポンプ20及び調整弁22を操作して処
理液溜2bに定量の処理液Lを溜め、ブロワ4を駆動し
て繊維製品Pの内側から外側へと気流を高圧で流す。同
時に循環ポンプ13及び熱交換器14を駆動して所定温
度の処理液Lを噴霧ノズル11から高圧気流中に噴射す
る。空気と霧状処理液の気液混合流体は、管路8からキ
ャリア3の基部3aを経て各スピンドル6内に導入さ
れ、スピンドル6の周面の多数の孔から噴出して繊維製
品Pの内側から外側へ貫流し、その過程で繊維製品Pを
染色する。製品Pの外周面から吹出した処理液Lは処理
液溜2bに流下して溜り、処理液循環路Bを経由して再
び噴霧ノズル11から噴射供給される。Processing of the package fiber product P by the processing apparatus 1 is performed as follows. First, the lid 2a of the processing tank 2 is opened to load the carrier 3 into the processing tank 2, and then the lid 2a is sealed. Next, the pump 20 and the regulating valve 22 are operated to store a fixed amount of the processing liquid L in the processing liquid reservoir 2b, and the blower 4 is driven to flow an air stream from the inside to the outside of the textile P at a high pressure. At the same time, the circulation pump 13 and the heat exchanger 14 are driven to inject the processing liquid L at a predetermined temperature from the spray nozzle 11 into a high-pressure airflow. A gas-liquid mixed fluid of air and mist treatment liquid is introduced into each spindle 6 from the pipe 8 through the base 3 a of the carrier 3, and is jetted out from a number of holes on the peripheral surface of the spindle 6 to the inside of the textile product P. From the outside and dyes the textile P in the process. The processing liquid L blown from the outer peripheral surface of the product P flows down and accumulates in the processing liquid reservoir 2b, and is again supplied from the spray nozzle 11 via the processing liquid circulation path B.
【0015】以上の実施例は気流をパッケージ繊維製品
Pの内側から外側に貫流させるいわゆるイン・アウト形
式の例であるが、これとは逆に外側から内側に流すアウ
ト・イン形式でも同様に処理が可能である。図2(A)
(B)はイン・アウトとアウト・インを切換可能にした
兼用タイプの処理装置1’である。この装置1’ではキ
ャリア3の入口開口部7に着脱自在に接続された配管2
5が処理槽2の中心線回りに回転可能に配設されてい
る。配管25は、軸26とリンク27を介して切換用シ
リンダ28に連結され、シリンダ28の作動により配管
25が半回転するように構成されている。処理槽2の下
部側壁には、入口開口部29と出口開口部30が180
°の角度差で対向して形成され、配管25が入口開口部
29又は出口開口部30に選択的に接続されるようにな
っている。The above embodiment is an example of a so-called in-out type in which air flows from the inside to the outside of the package fiber product P. Conversely, an out-in type in which air flows from the outside to the inside is similarly treated. Is possible. FIG. 2 (A)
(B) is a combined-type processing apparatus 1 'that can switch between in-out and out-in. In this apparatus 1 ′, a pipe 2 detachably connected to an inlet opening 7 of a carrier 3.
5 is disposed rotatably around the center line of the processing tank 2. The pipe 25 is connected to a switching cylinder 28 via a shaft 26 and a link 27, and is configured such that the pipe 25 makes a half turn by the operation of the cylinder 28. In the lower side wall of the processing tank 2, an inlet opening 29 and an outlet opening 30 are provided.
The pipes 25 are formed to face each other at an angle difference of ° so that the pipe 25 is selectively connected to the inlet opening 29 or the outlet opening 30.
【0016】出口開口部30は配管31、液溜32、配
管33、ブロワ4及び配管34を介して入口開口部29
に接続され、これらが気流循環路Aを形成している。ま
た処理液溜32はポンプ13、熱交換器14及び調整弁
15を介して処理液循環路Bにより配管34に挿入され
た噴霧ノズル11に接続されている。The outlet opening 30 is connected to the inlet opening 29 via a pipe 31, a liquid reservoir 32, a pipe 33, a blower 4 and a pipe 34.
And these form an air circulation circuit A. Further, the processing liquid reservoir 32 is connected to the spray nozzle 11 inserted into the pipe 34 by the processing liquid circulation path B via the pump 13, the heat exchanger 14, and the adjustment valve 15.
【0017】この兼用タイプの処理装置1’は、イン・
アウトとアウト・インを交互に切換えることにより、よ
り均一な処理を可能にする。イン・アウトの処理では、
図2(A)のようにブロワ4から吐出された気流に噴霧
ノズル11から霧状処理液が供給されて気液混合流体と
され、この気液混合流体が配管25を通ってキャリア3
のスピンドル6に供給される。スピンドル6の外周面の
多数の孔から出た気液混合流体は、パッケージ繊維製品
Pを内側から外側へ半径方向に貫流し、配管31を通っ
て処理液溜32に流入する。気流はさらに配管33を通
ってブロア4に吸入され、再びキャリア3に循環供給さ
れる。処理液は処理液溜32に一時的に貯溜された後、
ポンプ13、熱交換器14及び調整バルブ15を介して
噴霧ノズル11に循環供給される。This dual-purpose type processing apparatus 1 ′
By alternately switching out and out-in, more uniform processing is possible. In in-out processing,
As shown in FIG. 2 (A), the mist treatment liquid is supplied from the spray nozzle 11 to the gas flow discharged from the blower 4 to form a gas-liquid mixed fluid.
Is supplied to the spindle 6. The gas-liquid mixed fluid that has exited from the plurality of holes on the outer peripheral surface of the spindle 6 flows through the package fiber product P in the radial direction from the inside to the outside, and flows into the processing liquid reservoir 32 through the pipe 31. The airflow is further sucked into the blower 4 through the pipe 33 and is circulated to the carrier 3 again. After the processing liquid is temporarily stored in the processing liquid reservoir 32,
The fuel is circulated and supplied to the spray nozzle 11 via the pump 13, the heat exchanger 14, and the adjustment valve 15.
【0018】アウト・インの処理では、図2(B)のよ
うに配管25を半回転させて出口開口部30に接続して
おく。これにより入口開口部29から処理槽2内に供給
された気液混合流体が、パッケージ繊維製品Pの外側か
ら内側に半径方向に貫流し、この過程でパッケージ繊維
製品Pの処理がなされる。スピンドル6の内部に流入し
た気液混合流体は、配管31を通って処理液溜32に流
入する。気流と処理液は、その後図2(A)とまったく
同様に処理槽2の入口開口部29に循環供給される。こ
のように、気液混合流体の貫流方向を逆転させることに
より、パッケージ繊維製品Pに対する処理液の拡散を平
均化できて、より均一な処理がなされる。In the out-in process, the pipe 25 is rotated by a half turn as shown in FIG. As a result, the gas-liquid mixed fluid supplied into the processing tank 2 from the inlet opening 29 flows through the package fiber product P from the outside to the inside in the radial direction, and the package fiber product P is processed in this process. The gas-liquid mixed fluid flowing into the spindle 6 flows into the processing liquid reservoir 32 through the pipe 31. The airflow and the processing liquid are then circulated and supplied to the inlet opening 29 of the processing tank 2 in exactly the same manner as in FIG. In this way, by reversing the flow direction of the gas-liquid mixed fluid, the diffusion of the processing liquid to the package fiber product P can be averaged, and more uniform processing is performed.
【0019】なお、ブロワ4からの気流を加熱する加熱
手段を気流循環路Aに設ければ、霧状処理液を熱風によ
って繊維製品Pに固着処理することも可能である。If a heating means for heating the air flow from the blower 4 is provided in the air circulation circuit A, the mist-like treatment liquid can be fixed to the textile P by hot air.
【0020】[0020]
【発明の効果】本発明は前述の如く、処理槽内のパッケ
ージ繊維製品に霧状処理液を含む気液混合流体を貫流さ
せて処理するので、処理液が少量で済み、従来の限界で
あった1:6程度の低浴比をさらに推進して1:3以下
の超低浴比を可能にする。As described above, according to the present invention, since a gas-liquid mixed fluid containing a mist-like treatment liquid is caused to flow through a package fiber product in a treatment tank, the treatment is performed in a small amount, which is a limitation of the conventional art. Further, a low bath ratio of about 1: 6 is further promoted to enable an ultra low bath ratio of 1: 3 or less.
【図1】本発明の処理装置の概略断面図。FIG. 1 is a schematic sectional view of a processing apparatus of the present invention.
【図2】(A)及び(B)は、本発明の別の処理装置の
概略断面図。FIGS. 2A and 2B are schematic cross-sectional views of another processing apparatus of the present invention.
【図3】従来の処理装置の概略断面図。FIG. 3 is a schematic sectional view of a conventional processing apparatus.
1 竪型パッケージ染色処理装置 2 処理槽 2a 蓋 2b 処理液溜 3 キャリア 4 ブロワ 5 投入槽 6 スピンドル 8 配管 10 モータ 13 ポンプ 14 熱交換器 A 気流循環路 B 処理液循環路 P パッケージ繊維製品 DESCRIPTION OF SYMBOLS 1 Vertical package dyeing processing apparatus 2 Processing tank 2a lid 2b Processing liquid reservoir 3 Carrier 4 Blower 5 Input tank 6 Spindle 8 Piping 10 Motor 13 Pump 14 Heat exchanger A Air circulation circuit B Processing liquid circulation path P Package textile
Claims (1)
たスピンドルを多数並立設したキャリアを装填してなる
染色処理槽と、前記キャリアの内部空間と前記キャリア
の外部空間である処理槽とを、ブロワを有する気流循環
路で連通すると共に、前記パッケージ繊維製品を貫流し
た後の気流から分離された処理液を貯溜する液溜からポ
ンプ及び熱交換器を介して前記ブロワの吐出側気流循環
路に挿入した噴霧ノズルに至る処理液循環路を形成した
ことを特徴とする竪型パッケージ染色処理装置。1. A dyeing treatment tank loaded with a carrier in which a number of spindles stacked with packaged fiber products such as cheese are mounted in parallel, and a treatment tank which is an inner space of the carrier and an outer space of the carrier, While communicating with an airflow circuit having a blower, a pump and a heat exchanger are connected to a discharge-side airflow circuit of the blower from a liquid reservoir that stores a processing liquid separated from an airflow that has flowed through the package fiber product. A vertical package dyeing treatment apparatus characterized by forming a treatment liquid circulation path leading to the inserted spray nozzle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28935494A JP2609826B2 (en) | 1994-11-24 | 1994-11-24 | Vertical package dyeing processing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28935494A JP2609826B2 (en) | 1994-11-24 | 1994-11-24 | Vertical package dyeing processing equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08144169A JPH08144169A (en) | 1996-06-04 |
JP2609826B2 true JP2609826B2 (en) | 1997-05-14 |
Family
ID=17742122
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28935494A Expired - Fee Related JP2609826B2 (en) | 1994-11-24 | 1994-11-24 | Vertical package dyeing processing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2609826B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102134793A (en) * | 2011-04-15 | 2011-07-27 | 广州番禺高勋染整设备制造有限公司 | Ultralow bath-ratio yarn dyeing machine with three-level vane pump |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7140195B1 (en) * | 2005-10-14 | 2006-11-28 | Shields Fair | Heat transfer apparatus |
KR100944184B1 (en) * | 2008-02-12 | 2010-02-24 | (재)한국섬유기계연구소 | Spindle structure for uniformity yarn dyeing |
CN103726244B (en) * | 2014-01-06 | 2016-02-10 | 四川省宜宾惠美线业有限责任公司 | A kind of one-way circulation dyeing of cheese |
CN105887379A (en) * | 2014-11-21 | 2016-08-24 | 无锡市华洋染整机械有限公司 | Air flow and liquid flow dual-purpose spray nozzle of dyeing machine |
CN105951334A (en) * | 2016-07-26 | 2016-09-21 | 苏州科润织造有限公司 | Cone dyeing device |
KR101737875B1 (en) * | 2017-01-05 | 2017-05-19 | (주)대주기계 | Supercritical carbon dioxide dyeing bath for improvement of level dyeing |
-
1994
- 1994-11-24 JP JP28935494A patent/JP2609826B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102134793A (en) * | 2011-04-15 | 2011-07-27 | 广州番禺高勋染整设备制造有限公司 | Ultralow bath-ratio yarn dyeing machine with three-level vane pump |
Also Published As
Publication number | Publication date |
---|---|
JPH08144169A (en) | 1996-06-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3967923A (en) | Process for the wet treatment of textiles | |
JP3177736B2 (en) | Processing equipment | |
EP0711864B1 (en) | Dry-cleaning of garments using gas-jet agitation | |
JP3493030B2 (en) | Apparatus for processing substrates in a fluid container | |
JP2609826B2 (en) | Vertical package dyeing processing equipment | |
KR20010062026A (en) | Substrate processing apparatus | |
MX2009001885A (en) | Method for treating bottles or such like containers in a cleaning machine and also cleaning machine. | |
JPH05247832A (en) | Apparatus for wet treatment of textile product | |
SU946408A3 (en) | Apparatus for continuous liquid treatment of textile material | |
FI81133B (en) | FOERFARANDE FOER BEHANDLING AV FINFOERDELAT, FIBERFORMIGT CELLULOSAMATERIAL. | |
US6129451A (en) | Liquid carbon dioxide cleaning system and method | |
WO2003006183A2 (en) | Method and apparatus for cleaning semiconductor wafers and other flat media | |
CN219010686U (en) | Wheel inspection type dyeing machine | |
JPS6096255A (en) | Pressure kettle and sterilizing method | |
PL193751B1 (en) | Apparatus for treating liquids | |
JP2002081752A (en) | Heat recovery type heat storage apparatus | |
JP4020741B2 (en) | Gas-liquid separation and recovery equipment in liquid processing equipment | |
US4516413A (en) | Machines for the liquid or gaseous treatment of textile material or other fibrous or porous materials | |
KR20000013446A (en) | Wafer drying apparatus for fabricating of semiconductor device | |
JPS62162868A (en) | Evaporator | |
JP2004504504A (en) | Method and apparatus for continuously treating synthetic fibers in a heat exchange chamber | |
US5170523A (en) | Method and apparatus for wet processing of fabric | |
JPH04501892A (en) | Method and apparatus for processing material webs, especially textile webs | |
JP2769141B2 (en) | Vacuum processing method for fiber material and apparatus used therefor | |
US6233982B1 (en) | Method and device for the treatment of ready-to-wear, textile apparel parts |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19961210 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090213 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100213 Year of fee payment: 13 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100213 Year of fee payment: 13 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110213 Year of fee payment: 14 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110213 Year of fee payment: 14 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120213 Year of fee payment: 15 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130213 Year of fee payment: 16 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130213 Year of fee payment: 16 |
|
LAPS | Cancellation because of no payment of annual fees |