JP2765817B2 - Method for dissolving and supplying powdery drug and apparatus used therefor - Google Patents

Method for dissolving and supplying powdery drug and apparatus used therefor

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Publication number
JP2765817B2
JP2765817B2 JP3970996A JP3970996A JP2765817B2 JP 2765817 B2 JP2765817 B2 JP 2765817B2 JP 3970996 A JP3970996 A JP 3970996A JP 3970996 A JP3970996 A JP 3970996A JP 2765817 B2 JP2765817 B2 JP 2765817B2
Authority
JP
Japan
Prior art keywords
pipe
chemical
processing
processing liquid
liquid
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
Application number
JP3970996A
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Japanese (ja)
Other versions
JPH09228231A (en
Inventor
昌弘 米田
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.)
HISAKA SEISAKUSHO KK
Original Assignee
HISAKA SEISAKUSHO KK
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Priority to JP3970996A priority Critical patent/JP2765817B2/en
Publication of JPH09228231A publication Critical patent/JPH09228231A/en
Application granted granted Critical
Publication of JP2765817B2 publication Critical patent/JP2765817B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、繊維物に対し染
色,精練,漂白その他の処理を施す際に、染料,助剤等
の粉体状薬剤を液体に溶かして薬液とし、この薬液を処
理機に供給する粉体状薬剤の溶解供給方法およびそれに
用いる装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process for dissolving powdery chemicals such as dyes and auxiliaries into a liquid when dyeing, scouring, bleaching and other treatments of a fiber material, and treating the liquid chemical. TECHNICAL FIELD The present invention relates to a method for dissolving and supplying a powdery drug to be supplied to a machine and an apparatus used for the method.

【0002】[0002]

【従来の技術】従来から、染色機等の布帛処理機やパッ
ケージ処理機において、染色等の処理を行う際には、染
料や顔料,漂白剤,界面活性剤,精練剤等の粉体状薬剤
が用いられている。このような粉体状薬剤は、そのまま
処理機内に投入したのでは溶解や分散が不充分となって
処理むら等が生じる。このため、処理機とは別に投入槽
や攪拌設備等を設け、これらの設備により、粉体状薬剤
を一旦溶媒液に溶解して調整し、この調整済み薬液を処
理機の設置場所まで運搬して供給することが行われてい
る。
2. Description of the Related Art Conventionally, when performing processing such as dyeing in a cloth processing machine such as a dyeing machine or a package processing machine, powdery chemicals such as dyes and pigments, bleaching agents, surfactants and scouring agents are used. Is used. If such powdered chemicals are introduced into the processing machine as it is, dissolution or dispersion becomes insufficient and unevenness in processing occurs. For this reason, a charging tank and stirring equipment are provided separately from the processing machine, and these equipment are used to adjust the powdered chemical once dissolved in a solvent solution and transport this adjusted chemical solution to the installation location of the processing machine. Supply is being done.

【0003】このような処理機の一例を図9に示す。す
なわち、この装置は、いわゆる液流式の布帛処理機であ
り、41は布帛50が滞留する滞留槽で、42は上記布
帛50を移送する移送部である。上記滞留槽41と移送
部42とは、ほぼ平行に設置され、両端部で接続,連通
されて布帛50の循環処理通路を構成している。43は
上記滞留槽41の底部に3個所設けられた液吸込部であ
り、これら液吸込部43から吸い込まれた処理液は、ポ
ンプ45および熱交換器46を介してノズル44に至る
処理液循環路47によって循環するようになっている。
そして、48はこの処理機に薬液を供給するための薬液
槽であり、上記薬液槽48内の薬液は、ポンプ49を介
して処理液循環路47のポンプ45吸込側から処理機に
供給されるようになっている。
FIG. 9 shows an example of such a processor. That is, this apparatus is a so-called liquid flow type cloth processing machine, 41 is a stay tank in which the cloth 50 stays, and 42 is a transfer section for transferring the cloth 50. The stagnation tank 41 and the transfer section 42 are installed substantially in parallel, and connected and communicated at both ends to form a circulation processing passage for the fabric 50. Reference numeral 43 denotes three liquid suction portions provided at the bottom of the storage tank 41, and the processing liquid sucked from these liquid suction portions 43 circulates to the nozzle 44 via the pump 45 and the heat exchanger 46. It circulates by way 47.
Reference numeral 48 denotes a chemical tank for supplying a chemical to the processing machine. The chemical in the chemical tank 48 is supplied to the processing machine from the suction side of the pump 45 of the processing liquid circulation path 47 via the pump 49. It has become.

【0004】上記処理機に、処理液となる薬液を追加供
給する場合には、上述したように、この装置とは別個に
設けられた溶解設備等で、染料等の粉体状薬剤を水等に
溶解させて薬液とし、この処理機の設置場所まで運搬
し、上記薬液槽48に移し替えることが行われる。
[0004] When a chemical solution serving as a processing liquid is additionally supplied to the processing machine, as described above, a powdery chemical such as a dye is converted into water or the like by a dissolving facility or the like provided separately from this apparatus. Is dissolved in a chemical solution, transported to a place where the processing machine is installed, and transferred to the chemical solution tank 48.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
方法では、粉体状薬剤を溶解して薬液を調整するための
設備が、処理機以外に別途必要であり、その設備を設置
するためのスペースも必要になる。また、薬液の調整作
業や運搬作業が必要なだけでなく、投入槽や攪拌装置,
運搬容器の洗浄,保全等、付随する数々の作業も必要で
ある。さらに、薬液の運搬と移し替えを行うため、それ
に伴い薬液ロスも多い。このため、設備費や人件費,薬
液消費等が多大なものとなり、処理コストを引き上げる
大きな要因になっている。また、調整,攪拌,運搬の際
に、薬液が周囲に飛散して作業環境を汚染するという問
題もある。そのうえ、薬液が投入槽や攪拌装置に残留
し、その後に調整する薬液に上記残留薬液が混入して純
度の低下を招くといった問題も生じる。また、薬液が調
整されてから実際に布帛等と接触して処理されるまでの
間に、かなりの時間的な隔たりが生じることにより、特
に、反応性染料や酸性直接染料等のような経時変化の大
きな薬液では、その間に薬液の性状が変化し、処理むら
や処理不足の原因になる等の不都合も生じていた。
However, in the above-mentioned method, equipment for dissolving the powdery drug and adjusting the chemical solution is required separately from the processing machine, and a space for installing the equipment is required. Is also required. In addition, not only is the work of adjusting and transporting the chemical solution necessary, but also the charging tank, stirring device,
A number of incidental operations such as cleaning and maintenance of transport containers are also required. Furthermore, since the chemical solution is transported and transferred, the chemical solution loss is also large. For this reason, equipment costs, personnel costs, consumption of chemicals, and the like become enormous, which is a major factor in raising processing costs. In addition, there is also a problem that the chemical solution scatters around during the adjustment, agitation, and transportation to contaminate the working environment. In addition, there is a problem in that the chemical liquid remains in the charging tank or the stirring device, and the residual chemical liquid is mixed with the chemical liquid to be adjusted thereafter, thereby lowering the purity. In addition, there is a considerable time gap between the preparation of the chemical solution and the actual treatment by contacting with a cloth or the like, and particularly, a temporal change such as a reactive dye or an acid direct dye is caused. In the case of a large chemical solution, the properties of the chemical solution change during that time, causing inconvenience such as causing unevenness or insufficient treatment.

【0006】これらの問題を解消するためには、粉体状
薬剤を直接処理機に投入するのが望ましいのであるが、
上述したように、直接投入では粉体状薬剤の溶解や分散
が不充分であり、処理むらや処理不足等が生じる。この
ように、粉体状薬剤を直接投入できて、しかもその溶
解,分散を充分に行える供給方法は、現在のところ開発
されていないのが実情である。
[0006] In order to solve these problems, it is desirable to feed the powdered chemical directly into the processing machine.
As described above, if the powder is directly charged, the dissolution or dispersion of the powdered drug is insufficient, and uneven treatment or insufficient treatment occurs. As described above, a feeding method that can directly charge a powdery drug and sufficiently dissolve and disperse the drug has not been developed at present.

【0007】本発明は、このような事情に鑑みなされた
もので、粉体状薬剤を直接投入して溶解,分散させて処
理機に供給することができ、しかも、充分に溶解,分散
させることができる粉体状薬剤の溶解供給方法およびそ
れに用いる装置の提供をその目的とする。
The present invention has been made in view of such circumstances, and it is possible to supply a processing agent by dissolving and dispersing a powdered drug directly, and to sufficiently dissolve and disperse the same. It is an object of the present invention to provide a method for dissolving and supplying a powdery drug capable of producing a solution and an apparatus used therefor.

【0008】[0008]

【課題を解決するための手段】上記の目的を達成するた
め、本発明の粉体状薬剤の溶解供給方法は、ポンプを備
えた外部循環管路を介して処理液を循環することにより
処理槽の繊維製品を加工処理する方法において、密閉可
能に構成された投入槽内に染料,助剤等の粉体状薬剤を
投入し、上記循環管路のポンプ吐出側から処理液の一部
を取り出して、この処理液を旋回流として投入槽内に導
入して上記粉体状薬剤を溶解,分散させて薬液とし、こ
の薬液を薬液供給配管を介して上記循環管路のポンプ吸
込側に希釈供給し、かつ、上記循環管路のポンプ吐出側
から処理液の一部を取り出して上記薬液供給配管に還流
させ、還流配管と薬液供給配管との連通部において、還
流処理液を薬液供給配管の下流側に向かって噴射し、そ
の噴射流によるエジェクタ作用により、上流側の薬液を
随伴吸引するとともに薬液の溶解,分散を促進するよう
にしたことを要旨とする。
In order to achieve the above object, the present invention provides a method for dissolving and supplying a powdery drug, comprising the steps of: circulating a processing solution through an external circulation pipe provided with a pump; In the method for processing textile products, powdery chemicals such as dyes and auxiliaries are charged into a charging tank configured to be hermetically sealed, and a part of the processing liquid is taken out from the pump discharge side of the circulation pipe. The treatment liquid is introduced as a swirling flow into the charging tank to dissolve and disperse the powdered drug into a drug solution, and the drug solution is diluted and supplied to the pump suction side of the circulation line via a drug solution supply pipe. And, a part of the treatment liquid is taken out from the pump discharge side of the circulation pipe and is returned to the chemical supply pipe, and at a communication portion between the reflux pipe and the chemical supply pipe, the reflux treatment liquid is downstream of the chemical supply pipe. Side, and the The Ekuta action, dissolution of the chemical with the upstream side of the chemical liquid accompanying the suction is summarized in that which is adapted to facilitate dispersion.

【0009】また、本発明の粉体状薬剤の溶解供給装置
は、ポンプを備えた外部循環管路を介して処理液を循環
することにより処理槽の繊維製品を加工処理する装置に
おいて、密閉可能に構成され染料,助剤等の粉体状薬剤
が投入される投入槽と、上記循環管路のポンプ吐出側か
ら分岐して上記投入槽へ連通する処理液導入配管と、上
記処理液導入配管と投入槽との連通部に設けられ処理液
を旋回流として導入させて投入槽内部の粉体状薬剤を溶
解,分散させる旋回流導入ノズルと、上記投入槽から上
記循環管路のポンプ吸込側に接続される薬液供給配管と
を備え、上記循環管路のポンプ吐出側から分岐して上記
薬液供給配管に延びる還流配管を設け、この還流配管と
薬液供給配管との連通部に、還流処理液を薬液供給配管
の下流側に向かって噴射してその噴射流により上流側の
薬液を随伴吸引するとともに薬液の溶解,分散を促進す
るエジェクタ手段を設けたことを要旨とする。
Further, the powdery drug dissolution supply apparatus of the present invention can be hermetically sealed in an apparatus for processing and processing textile products in a processing tank by circulating a processing liquid through an external circulation pipe provided with a pump. A charging tank into which powdery chemicals such as dyes and auxiliaries are charged, a processing liquid introducing pipe branched from the pump discharge side of the circulation pipe and communicating with the charging tank, and a processing liquid introducing pipe A swirl flow introducing nozzle provided in a communication portion between the charging tank and the charging tank to introduce a processing liquid as a swirling flow to dissolve and disperse the powdered medicine in the charging tank; A liquid supply pipe connected to the pump, and a return pipe branched from the pump discharge side of the circulation pipe and extending to the liquid supply pipe. A communication section between the return pipe and the liquid supply pipe is provided with a reflux treatment liquid. To the downstream side of the chemical supply pipe. Injection to dissolve the drug solution with the upstream side of the chemical liquid accompanying the suction by the jet, is summarized as providing the ejector means to promote dispersion.

【0010】すなわち、本発明は、循環管路のポンプ吐
出側から処理液の一部を取り出して投入槽内に導入し、
この導入処理液で投入槽に投入された粉体状薬剤を溶
解,分散させて薬液とし、この薬液を薬液供給配管を介
して上記循環管路のポンプ吸込側に希釈供給するように
している。したがって、従来のような薬剤調整設備を用
いることなく、粉体状薬剤を直接投入し、この粉体状薬
剤を溶解させて薬液として処理機に供給することができ
る。このため、薬液を調整するための設備が不要で、そ
の設置スペースも不要になる。また、薬液調整作業や運
搬作業、それに付随する種々の作業も不要になる。さら
に、薬液の運搬も移し替えも行わないことから、薬液ロ
スもない。このため、設備費や人件費,薬液消費等が削
減され、処理コストを大幅に低下させることができる。
また、薬液が周囲に飛散せず、作業環境も良好になるう
え、残留薬液が混入して純度が低下することもない。し
かも、粉体状薬剤が溶解されて薬液化してから、きわめ
て短時間で布帛等と接触して処理されるため、反応性染
料や酸性直接染料等を用いる場合でも処理前に薬液の性
状が変化せず、処理むらや処理不足が生じなくなる。
That is, according to the present invention, a part of the processing liquid is taken out from the pump discharge side of the circulation pipe and introduced into the charging tank.
The powdery chemicals charged into the charging tank are dissolved and dispersed with the introduction processing liquid to be a chemical liquid, and the chemical liquid is diluted and supplied to the pump suction side of the circulation pipe via the chemical liquid supply pipe. Therefore, a powdery medicine can be directly introduced, and the powdery medicine can be dissolved and supplied to the processing machine as a chemical liquid without using a conventional medicine adjusting equipment. For this reason, equipment for adjusting the chemical solution is not required, and the installation space is also unnecessary. Further, the chemical solution adjusting operation, the transporting operation, and various operations associated therewith become unnecessary. Further, no chemical solution is transported or transferred, so that there is no chemical solution loss. For this reason, equipment costs, personnel costs, consumption of chemicals, and the like are reduced, and processing costs can be significantly reduced.
In addition, the chemical solution does not scatter to the surroundings, the working environment is improved, and the purity does not decrease due to mixing of the residual chemical solution. In addition, since the powdered drug is dissolved and converted into a chemical solution, it is processed in a very short time by contacting with a cloth or the like. Therefore, even when a reactive dye or an acidic direct dye is used, the property of the chemical solution changes before the treatment. As a result, uneven processing and insufficient processing do not occur.

【0011】また、本発明は、まず、処理液を旋回流と
して投入槽内に導入し、投入槽内の粉体状薬剤を溶解,
分散させて薬液とする。そして、この薬液を循環管路の
ポンプ吸込側に供給する際、循環管路のポンプ吐出側か
ら処理液の一部を薬液供給配管に還流させ、還流配管と
薬液供給配管との連通部において、還流処理液を薬液供
給配管の下流側に向かって噴射し、その噴射流によるエ
ジェクタ作用により、上流側の薬液を随伴吸引するとと
もに、上記薬液の溶解,分散を促進するようにしてい
る。このように、投入槽内に、処理液の旋回流により渦
流を生じさせ、この渦流により投入槽内を攪拌して粉体
状薬剤を溶解,分散させる。そして、それによって得ら
れた薬液を、処理液の噴射流によるエジェクタ作用でさ
らに溶解,分散させるようにしている。したがって、上
記2段階の溶解,分散を行うことにより、粉体状薬剤を
直接投入する方式において従来問題視されていた溶解不
良が起こらず、粉体状薬剤が充分に溶解,分散されるよ
うになる。このため、処理むらや処理不足がなく、高品
質の安定した処理を行うことができるようになる。
Further, according to the present invention, first, the treatment liquid is introduced into the charging tank as a swirling flow, and the powdered drug in the charging tank is dissolved and dissolved.
Disperse to make a drug solution. Then, when supplying this chemical solution to the pump suction side of the circulation pipe, a part of the processing liquid is returned to the chemical supply pipe from the pump discharge side of the circulation pipe, and at the communication portion between the reflux pipe and the chemical supply pipe, The reflux treatment liquid is jetted toward the downstream side of the chemical supply pipe, and the ejector action by the jet flow sucks the chemical at the upstream side and promotes the dissolution and dispersion of the chemical. As described above, a vortex is generated in the charging tank by the swirling flow of the processing liquid, and the powder is dissolved and dispersed by stirring the charging tank by the vortex. Then, the obtained chemical liquid is further dissolved and dispersed by an ejector action by the jet flow of the processing liquid. Therefore, by performing the above-described two-stage dissolution and dispersion, the poor dissolution which has been regarded as a problem in the method of directly charging the powdered drug does not occur, and the powdered drug is sufficiently dissolved and dispersed. Become. Therefore, high-quality stable processing can be performed without processing unevenness or processing shortage.

【0012】しかも、粉体状薬剤を一旦投入槽で溶解し
て薬液とし、その薬液をエジェクタ部において還流処理
液で希釈し、さらにそれを循環管路のポンプ吸込側に供
給して大量の循環処理液中に合流させることにより希釈
する。このように、粉体状薬剤を溶解した高濃度の薬液
を、所定の濃度に希釈した処理液として処理機に供給す
ることができる。このため、例えば、粉体状薬剤を循環
管路に直接投入した場合のように、部分的に極端に濃度
の高い薬液が循環して処理むらを引き起こすようなこと
もない。
In addition, the powdered drug is once dissolved in a charging tank to form a drug solution, and the drug solution is diluted with a reflux treatment solution in an ejector section, and the diluted solution is supplied to a pump suction side of a circulation pipe to provide a large amount of circulation. It is diluted by merging into the processing solution. As described above, a high-concentration chemical solution in which a powdery drug is dissolved can be supplied to a processing machine as a processing solution diluted to a predetermined concentration. For this reason, for example, unlike the case where the powdered drug is directly introduced into the circulation pipe, the extremely high concentration of the drug solution does not partially circulate, thereby causing processing unevenness.

【0013】また、本発明において、処理液を旋回流と
して投入槽内に導入する際、導入処理液を2個所のノズ
ルから右旋回流および左旋回流として交互にもしくは同
時に導入するようにした場合には、投入槽内に渦流だけ
でなく乱流を生じさせることができる。これにより、攪
拌作用がより強力になって粉体状薬剤の溶解,分散がさ
らに促進され、より一層安定した処理を行うことができ
るようになる。
In the present invention, when the processing liquid is introduced into the charging tank as a swirling flow, the introduced processing liquid is alternately or simultaneously introduced as a right swirling flow and a left swirling flow from two nozzles. Can generate not only a vortex but also a turbulent flow in the charging tank. As a result, the stirring action becomes stronger, and the dissolution and dispersion of the powdered drug are further promoted, so that a more stable treatment can be performed.

【0014】[0014]

【発明の実施の形態】つぎに、本発明の実施の形態を詳
しく説明する。
Next, embodiments of the present invention will be described in detail.

【0015】図1は、本発明の一実施の形態例の粉体状
薬剤の溶解供給装置を示す。図において、10は処理機
(図示せず)に付設された循環管路であり、ポンプ11
の吐出力によって図示の右側から左側に向かって処理液
が循環するようになっている。1は投入槽であり、この
投入槽1の側壁部には、上記循環管路10のポンプ11
吐出側から分岐する処理液導入配管2が連通している。
この処理液導入配管2は、先端側が三方口弁12を介し
て二又に分岐しており、そのそれぞれに旋回流導入ノズ
ル5a,5bが設けられている。上記処理液導入配管2
には、循環仕切弁15が設けられている。また、この投
入槽1の底部には、薬液供給配管3が連通し、この薬液
供給配管3が上記循環管路10のポンプ11吸込側に接
続されている。そして、上記投入槽1内に粉体状薬剤が
投入され、槽内に導入される処理液によって溶解,分散
されて薬液となり、この薬液が薬液供給配管3から処理
機の循環管路10に希釈供給されるようになっている。
図において、13は投入槽1の上面を開閉しうる蓋であ
り、外周にリング13aが締め付けられて投入槽1を密
閉するようになっている。また、14は投入槽1内の圧
力を抜いて上記蓋13の開閉を容易にする空気抜き弁で
ある。なお、上記蓋13は、導入処理液の液漏れ等を防
ぐため、密閉することが好ましいが、密閉しなくても差
し支えなく、蓋13を使用しなくてもよい。
FIG. 1 shows an apparatus for dissolving and supplying a powdered drug according to an embodiment of the present invention. In the figure, reference numeral 10 denotes a circulation line attached to a processing machine (not shown), and a pump 11
The processing liquid circulates from the right side to the left side in the drawing by the discharge force of the liquid. Reference numeral 1 denotes a charging tank, and a pump 11 of the circulation line 10 is provided on a side wall of the charging tank 1.
A processing liquid introduction pipe 2 branched from the discharge side communicates with the processing liquid introduction pipe 2.
The treatment liquid introduction pipe 2 is bifurcated at the tip end via a three-way valve 12, and is provided with swirl flow introduction nozzles 5 a and 5 b, respectively. The above treatment liquid introduction pipe 2
Is provided with a circulation gate valve 15. A chemical supply pipe 3 communicates with the bottom of the charging tank 1, and the chemical supply pipe 3 is connected to the pump 11 suction side of the circulation line 10. Then, the powdered chemical is charged into the charging tank 1 and dissolved and dispersed by the processing liquid introduced into the tank to become a chemical, and this chemical is diluted from the chemical supply pipe 3 to the circulation line 10 of the processing machine. It is being supplied.
In the figure, reference numeral 13 denotes a lid capable of opening and closing the upper surface of the charging tank 1, and a ring 13a is fastened to the outer periphery to seal the charging tank 1. Reference numeral 14 denotes an air vent valve for releasing the pressure in the charging tank 1 to facilitate opening and closing of the lid 13. The lid 13 is preferably hermetically sealed in order to prevent leakage of the introduction treatment liquid, but it is not necessary to seal the lid 13 and the lid 13 may not be used.

【0016】上記旋回流導入ノズル5a,5bは、図2
に示すように、一方(図2において上側)が処理液を右
旋回流(図示の矢印A)として導入する右旋回流導入ノ
ズル5aであり、他方(図2において下側)が処理液を
左旋回流(図示の矢印B)として導入する左旋回流導入
ノズル5bである。そして、上記三方口弁12の切替え
制御により、右旋回流と左旋回流とが交互にもしくは同
時に導入され、この導入処理液の旋回流によって投入槽
1内に渦流,乱流を発生させ、積極的に攪拌し、槽内に
投入された粉体状薬剤を溶解,分散させるようになって
いる。なお、上記両旋回流導入ノズル5a,5bは、い
ずれか一方を単独で用いるようにしても差し支えない。
The above-mentioned swirling flow introducing nozzles 5a and 5b are shown in FIG.
As shown in FIG. 2, one (upper side in FIG. 2) is a right swirling flow introducing nozzle 5a that introduces the processing liquid as a right swirling flow (arrow A in the drawing), and the other (lower side in FIG. 2) swirls the processing liquid left. This is a left swirling flow introducing nozzle 5b that is introduced as a circulating flow (arrow B in the drawing). By the switching control of the three-way port valve 12, a right swirling flow and a left swirling flow are alternately or simultaneously introduced, and a swirling flow and a turbulent flow are generated in the charging tank 1 by the swirling flow of the introduced processing liquid. To dissolve and disperse the powdered drug charged into the tank. It should be noted that one of the two swirling flow introducing nozzles 5a and 5b may be used alone.

【0017】この装置には、上記循環管路10のポンプ
11吐出側から分岐して上記薬液供給配管3に還流する
還流配管7が設けられている(図1に戻る)。そして、
この還流配管7と薬液供給配管3の連通部には、エジェ
クタ部4が設けられている。このエジェクタ部4は、図
3に示すように、還流配管7と薬液供給配管3との連通
部に液密状のケース8が設けられ、上記ケース8の天井
壁と底壁に、それぞれ薬液供給配管3の上流側配管3a
および下流側配管3bが連通している。そして、上記ケ
ース8の側壁に還流配管7が液密状に貫通して下方に向
かって折曲げ形成され、その先端部が上記下流側配管3
bの連通部近傍まで延長されるとともに、この先端が還
流処理液の噴射ノズル30に形成されている。このエジ
ェクタ部4では、還流配管7からの還流処理液が噴射ノ
ズル30から噴射され、この噴射力によってケース8内
の薬液を随伴吸引しながら下流側配管3b内に噴射する
(エジェクタ作用)。そして、上記薬液と処理液とが激
しく攪拌され、溶解,分散が促進されるようになってい
る。また、上記還流配管7には、流量調節弁17が設け
られており(図1に戻る)、還流処理液の流量を調節し
てエジェクタ部4での噴射力を調節できるようになって
いる。図1において、9は薬液供給配管3の上流側配管
3aに設けられた注入仕切弁である。
This apparatus is provided with a return pipe 7 that branches off from the pump 11 discharge side of the circulation pipe 10 and returns to the chemical supply pipe 3 (return to FIG. 1). And
An ejector unit 4 is provided at a communication part between the reflux pipe 7 and the chemical supply pipe 3. As shown in FIG. 3, the ejector unit 4 is provided with a liquid-tight case 8 at a communication portion between the reflux pipe 7 and the chemical supply pipe 3, and the liquid supply case 8 is provided on a ceiling wall and a bottom wall of the case 8, respectively. Upstream pipe 3a of pipe 3
And the downstream pipe 3b are in communication with each other. A reflux pipe 7 penetrates through the side wall of the case 8 in a liquid-tight manner and is bent downward.
In addition to the extension to the vicinity of the communicating portion b, the tip is formed in the injection nozzle 30 of the reflux processing liquid. In the ejector unit 4, the reflux processing liquid from the reflux pipe 7 is injected from the injection nozzle 30, and is injected into the downstream pipe 3 b while sucking the chemical solution in the case 8 by the injection force (ejector action). Then, the chemical solution and the treatment solution are vigorously stirred to promote dissolution and dispersion. The reflux pipe 7 is provided with a flow rate control valve 17 (return to FIG. 1) so that the flow rate of the reflux processing liquid can be adjusted to adjust the injection force at the ejector unit 4. In FIG. 1, reference numeral 9 denotes an injection gate valve provided on the upstream pipe 3a of the chemical supply pipe 3.

【0018】上記構成の粉体状薬剤の溶解供給装置を用
いて、粉体状薬剤の溶解,供給はつぎのようにして行わ
れる。
The dissolving and supplying of the powdered medicine is performed as follows using the dissolving and supplying device for the powdered medicine having the above-mentioned structure.

【0019】まず、投入槽1の蓋13を開け、投入槽1
中に染料,助剤等の粉体状薬剤を投入し、蓋13を閉じ
てリング13aを締め付け、密閉する。ついで、空気抜
き弁14を閉じるとともに、循環仕切弁15を開け、循
環管路10の処理液の一部を投入槽1内に導入する。こ
の導入の際、三方口弁12を切替え制御することによ
り、右旋回流導入ノズル5aと左旋回流導入ノズル5b
を交互に切替え、右旋回流と左旋回流が交互に導入され
る。これにより投入槽1内に渦流や乱流が生じて攪拌さ
れ、内部の粉体状薬剤を溶解,分散させて薬液とする。
First, the lid 13 of the charging tank 1 is opened, and the charging tank 1 is opened.
A powdery drug such as a dye or an auxiliary agent is charged therein, the lid 13 is closed, and the ring 13a is tightened to seal. Next, the air vent valve 14 is closed, the circulation gate valve 15 is opened, and a part of the processing liquid in the circulation pipeline 10 is introduced into the charging tank 1. At the time of this introduction, the three-way valve 12 is switched and controlled, so that the right swirl flow introducing nozzle 5a and the left swirl flow introducing nozzle 5b are controlled.
Are alternately switched, and the right swirling flow and the left swirling flow are alternately introduced. As a result, a vortex or a turbulent flow is generated in the charging tank 1 and agitated, and the powdered medicine inside is dissolved and dispersed to form a drug solution.

【0020】つぎに、投入槽1内が処理液で満たされる
と、注入仕切弁9を開け、投入槽1内の薬液を薬液供給
配管3を通して循環管路10のポンプ11吸込側に供給
する。このとき、エジェクタ部4内において、上述した
エジェクタ作用により薬液供給配管3の上流側配管3a
の薬液が随伴吸引され、還流処理液とともに下流側配管
3b内に噴射され、上記薬液の溶解,分解が促進され
る。また、投入槽1内の高濃度の薬液は、エジェクタ作
用により還流処理液と混ざり、希釈されることになる。
そして、この希釈された薬液は、循環管路10のポンプ
11吸込側に供給され、循環管路10内を循環する大量
の循環処理液と合流してさらに希釈され、ポンプ11に
吸い込まれてその回転により攪拌されて所定の濃度にな
って循環管路10内を循環し、処理機に供給される。
Next, when the charging tank 1 is filled with the processing liquid, the injection gate valve 9 is opened, and the chemical liquid in the charging tank 1 is supplied to the pump 11 suction side of the circulation pipe 10 through the chemical liquid supply pipe 3. At this time, in the ejector section 4, the upstream side pipe 3 a of the chemical solution supply pipe 3 is formed by the above-described ejector action.
Of the chemical is sucked and injected into the downstream pipe 3b together with the reflux treatment liquid, so that the chemical is dissolved and decomposed. In addition, the high-concentration chemical solution in the charging tank 1 is mixed and diluted with the reflux treatment liquid by the ejector action.
Then, the diluted chemical is supplied to the suction side of the pump 11 of the circulation line 10, merges with a large amount of the circulating treatment liquid circulating in the circulation line 10, is further diluted, and is sucked into the pump 11. The mixture is agitated by rotation to reach a predetermined concentration, circulates in the circulation line 10, and is supplied to the processing machine.

【0021】そののち、循環仕切弁15を閉じて投入槽
1内への処理液の導入を止め、投入槽1内の薬液を供給
し終わったのち、注入仕切弁9を閉じる。そして、空気
抜き弁14を開けて投入槽1内の圧力を抜き、蓋13を
開けることができる状態にして、一連の粉体状薬剤の溶
解供給が終了する。
Thereafter, the circulation gate valve 15 is closed to stop the introduction of the processing liquid into the charging tank 1, and after the supply of the chemical solution in the charging tank 1 is completed, the injection gate valve 9 is closed. Then, the air release valve 14 is opened to release the pressure in the charging tank 1 so that the lid 13 can be opened, and a series of dissolution and supply of the powdered medicine is completed.

【0022】このような粉体状薬剤の溶解供給装置は、
例えば、図4に示すように、液流式布帛処理機に適用す
ることができる。すなわち、図において、21は布帛2
8が滞留する滞留槽で、22は上記布帛28を移送する
移送部である。上記滞留槽21と移送部22とは両端部
で接続,連通されて布帛28の循環処理通路を構成して
いる。23は上記滞留槽21の底部に4個所設けられた
液吸込部であり、これら液吸込部23から吸い込まれた
処理液が、ポンプ25および熱交換器26を経てノズル
24に至る循環管路27によって循環するようになって
いる。そして、本発明の装置は、上記循環管路27に付
設され、循環管路27のポンプ25吐出側から処理液を
投入槽1内に導入して薬液とするとともに、この薬液を
エジェクタ4を介してさらに溶解,分散させながら上記
循環管路27のポンプ25吸込側に供給し、処理機に追
加供給するようになっている。
Such a powdery drug dissolving and supplying apparatus is
For example, as shown in FIG. 4, the present invention can be applied to a liquid flow type cloth processing machine. That is, in the figure, 21 is cloth 2
Reference numeral 8 denotes a retention tank in which the cloth 28 is transported. The storage tank 21 and the transfer section 22 are connected and communicated at both ends to form a circulation processing passage for the cloth 28. Reference numeral 23 denotes four liquid suction sections provided at the bottom of the storage tank 21. The processing liquid sucked from the liquid suction sections 23 is circulated through a pump 25 and a heat exchanger 26 to a circulation pipe 27 reaching the nozzle 24. It is designed to circulate. The apparatus of the present invention is attached to the circulation line 27, and introduces the processing liquid into the charging tank 1 from the discharge side of the pump 25 of the circulation line 27, converts the processing liquid into the charging tank 1, and supplies the processing liquid via the ejector 4. Further, while further dissolving and dispersing, it is supplied to the suction side of the pump 25 of the circulation pipe 27, and is additionally supplied to the processing machine.

【0023】このように、上記粉体状薬剤の溶解供給装
置によれば、粉体状薬剤を投入槽1に直接投入するだけ
で、この粉体状薬剤を溶解して処理機に供給することが
できるようになる。また、粉体状薬剤を、処理液の旋回
流により投入槽1内で一旦溶解,分散させて薬液とし、
この薬液を、エジェクタ作用によりさらに溶解,分散さ
せる。このように、2段階の溶解,分散作用を行うこと
により、粉体状薬剤を充分に溶解,分散するようになっ
ている。しかも、処理液を2個所の旋回流導入ノズル5
a,5bから右旋回流と左旋回流とで交互に導入するた
め、投入槽1内に渦流や乱流を生じ、強力に攪拌するこ
とができる。
As described above, according to the powdery medicine dissolving and supplying apparatus, the powdery medicine is dissolved and supplied to the processing machine only by directly charging the powdery medicine into the charging tank 1. Will be able to Further, the powdered chemical is once dissolved and dispersed in the charging tank 1 by the swirling flow of the processing liquid to form a chemical,
This chemical solution is further dissolved and dispersed by an ejector action. As described above, by performing the two-stage dissolving and dispersing action, the powdered drug is sufficiently dissolved and dispersed. Moreover, the processing liquid is supplied to the two swirl flow introducing nozzles 5.
Since the swirling flow and the left swirling flow are alternately introduced from a and 5b, a vortex or a turbulent flow is generated in the charging tank 1, and strong stirring can be performed.

【0024】図5は、本発明の粉体状薬剤の溶解供給装
置を気流式布帛処理機に適用した一例を示している。す
なわち、この気流式布帛処理機には、処理機の底部から
吸い込まれた処理液をポンプ20によって処理機の上部
に向かって循環させる循環管路19が設けられている。
そして、この循環管路19に本発明の装置が付設されて
いる。この場合にも、図4に示すものと同様の作用,効
果を奏する。
FIG. 5 shows an example in which the apparatus for dissolving and supplying a powdery drug of the present invention is applied to an airflow type cloth processing machine. That is, the airflow type cloth processing machine is provided with the circulation pipe line 19 for circulating the processing liquid sucked from the bottom of the processing machine toward the upper part of the processing machine by the pump 20.
The apparatus of the present invention is attached to the circulation line 19. In this case, the same operation and effect as those shown in FIG.

【0025】なお、上記両適用例では、本発明の装置を
布帛処理機に適用した例を示したが、これに限定される
ものではなく、チーズ等を染色処理するチーズ染色機等
に適用してもよい。すなわち、本発明の装置は、処理機
の外部に、ポンプを介して処理液を循環させる循環管路
を有する処理機であれば、その循環管路に付設して適用
することができる。
In both the above-mentioned application examples, an example in which the apparatus of the present invention is applied to a cloth processing machine is shown. However, the present invention is not limited to this, and is applied to a cheese dyeing machine for dyeing cheese or the like. You may. That is, the apparatus of the present invention can be applied to a processing machine having a circulation pipe for circulating a processing liquid via a pump outside the processing machine, by attaching it to the circulation pipe.

【0026】図6は、本発明の第2の実施の形態例を示
している。すなわち、この装置では、処理液導入配管2
が二又に分岐し、それぞれの分岐管に開閉弁16を介し
て旋回流導入ノズル5a,5bが取り付けられ、上記開
閉弁16を切替え制御するようになっている。それ以外
は図1に示す装置と同様であり、同一部分には同一符号
を付している。この装置でも図1の装置と同様の作用,
効果を奏する。
FIG. 6 shows a second embodiment of the present invention. That is, in this apparatus, the processing liquid introduction pipe 2
Are branched into two branches, and swirl flow introducing nozzles 5a, 5b are attached to the respective branch pipes via opening / closing valves 16, so that the opening / closing valves 16 are switched. The other parts are the same as those of the apparatus shown in FIG. 1, and the same parts are denoted by the same reference numerals. This device operates in the same manner as the device of FIG.
It works.

【0027】なお、上記各実施の形態例では、旋回流導
入ノズル5a,5bから投入槽1内に導入される処理液
の旋回流を、右旋回流と左旋回流とで交互に切り換えて
投入槽1内を攪拌するようにしたが、上記右旋回流と左
旋回流とを同時に導入することにより投入槽1内を攪拌
するようにしてもよい。
In each of the above embodiments, the swirling flow of the processing liquid introduced from the swirling flow introducing nozzles 5a and 5b into the charging tank 1 is alternately switched between a right swirling flow and a left swirling flow. Although the inside of the charging tank 1 is agitated, the inside of the charging tank 1 may be stirred by simultaneously introducing the right swirling flow and the left swirling flow.

【0028】図7は、本発明の第3の実施の形態例のエ
ジェクタ部4aを示している。すなわち、このエジェク
タ部4aは、還流配管7aと薬液供給配管3との連通部
に液密状のケース8aが設けられ、このケース8aの側
壁に還流配管7aが連通し、天井壁と底壁とに、それぞ
れ薬液供給配管3の上流側配管3aと下流側配管3bが
接続されている。そして、上記上流側配管3aは、ケー
ス8aの天井壁を貫通してケース8a内を垂下し、その
下端6が底壁の下流側配管3b連通部の近傍まで延長さ
れている。このエジェクタ部4aでは、還流配管7aか
らケース8a内に流入した還流処理液が、上記上流側配
管3aの下端6と下流側配管3bの連通部との隙間18
から下流側配管3b内に噴射され、その噴射力によって
上流側配管3a内の薬液が随伴吸引される。そして、こ
こで随伴吸引された薬液が還流処理液とともに下流側配
管3b内に噴射される際に、その噴射力により上記薬液
と処理液とが激しく攪拌され、その溶解,分散が促進さ
れるとともに希釈されるようになっている。
FIG. 7 shows an ejector unit 4a according to a third embodiment of the present invention. That is, in the ejector portion 4a, a liquid-tight case 8a is provided at a communication portion between the reflux pipe 7a and the chemical solution supply pipe 3, and a reflux pipe 7a communicates with a side wall of the case 8a. Are connected to an upstream pipe 3a and a downstream pipe 3b of the chemical liquid supply pipe 3, respectively. The upstream pipe 3a penetrates the ceiling wall of the case 8a and hangs down in the case 8a. The lower end 6 of the upstream pipe 3a is extended to the vicinity of the downstream pipe 3b communicating with the bottom wall. In the ejector section 4a, the reflux processing liquid flowing into the case 8a from the reflux pipe 7a is filled with a gap 18 between the lower end 6 of the upstream pipe 3a and the communication section between the downstream pipe 3b.
Is injected into the downstream pipe 3b, and the chemical force in the upstream pipe 3a is sucked by the injection force. When the chemical solution sucked here is injected into the downstream pipe 3b together with the reflux processing liquid, the chemical liquid and the processing liquid are vigorously stirred by the injection force, and the dissolution and dispersion thereof are promoted. It is intended to be diluted.

【0029】図8は、本発明の第4の実施の形態例のエ
ジェクタ部4bを示している。すなわち、このエジェク
タ部4bは、還流配管7bと薬液供給配管3との連通部
にケースが設けられておらず、上記薬液供給配管3の側
壁に還流配管7bが液密状に貫通して下流側に向かって
折曲げ形成され、その先端が還流処理液の噴射ノズル3
0aに形成されている。このエジェクタ部4bでも、還
流配管7bからの還流処理液が噴射ノズル30aから噴
射され、この噴射力によって薬液供給配管3内の薬液を
随伴吸引する(エジェクタ作用)。そして、ここで随伴
吸引された薬液が還流処理液とともに噴射される際に、
その噴射力により上記薬液と処理液とが激しく攪拌さ
れ、その溶解,分散が促進されるとともに希釈されるよ
うになっている。
FIG. 8 shows an ejector unit 4b according to a fourth embodiment of the present invention. That is, in the ejector portion 4b, a case is not provided at a communication portion between the reflux pipe 7b and the chemical supply pipe 3, and the reflux pipe 7b penetrates the side wall of the chemical supply pipe 3 in a liquid-tight manner and the downstream side. Formed at the tip of the nozzle 3
0a. In the ejector section 4b as well, the reflux treatment liquid from the reflux pipe 7b is ejected from the ejection nozzle 30a, and the ejection force causes the chemical solution in the chemical solution supply pipe 3 to be sucked accompanying (ejector action). And, when the chemical liquid sucked here is injected together with the reflux treatment liquid,
The jetting force violently agitates the chemical solution and the processing liquid to promote their dissolution and dispersion and to dilute them.

【0030】[0030]

【発明の効果】以上のように、本発明によれば、従来の
ような薬液調整設備を用いることなく、粉体状薬剤を直
接投入し、この粉体状薬剤を溶解させて薬液として処理
機に供給することができる。このため、薬液を調整する
ための設備が不要で、その設置スペースも不要になる。
また、薬液調整作業や運搬作業、それに付随する種々の
作業も不要になる。さらに、薬液の運搬も移し替えも行
わないことから、薬液ロスもない。このため、設備費や
人件費,薬液消費等が削減され、処理コストを大幅に低
下させることができる。また、薬液が周囲に飛散せず、
作業環境も良好になるうえ、残留薬液が混入して純度が
低下することもない。しかも、粉体状薬剤が溶解されて
薬液化してから、きわめて短時間で布帛等と接触して処
理されるため、反応性染料や酸性直接染料等を用いる場
合でも処理前に薬液の性状が変化せず、処理むらや処理
不足が生じなくなる。
As described above, according to the present invention, a powdery medicine is directly charged without using a conventional chemical liquid adjustment equipment, and this powdery medicine is dissolved to produce a processing liquid as a chemical liquid. Can be supplied to For this reason, equipment for adjusting the chemical solution is not required, and the installation space is also unnecessary.
Further, the chemical solution adjusting operation, the transporting operation, and various operations associated therewith become unnecessary. Further, no chemical solution is transported or transferred, so that there is no chemical solution loss. For this reason, equipment costs, personnel costs, consumption of chemicals, and the like are reduced, and processing costs can be significantly reduced. Also, the chemical does not scatter around,
The working environment is improved, and the purity does not decrease due to mixing of the residual chemical liquid. In addition, since the powdered drug is dissolved and converted into a chemical solution, it is processed in a very short time by contacting with a cloth or the like. Therefore, even when a reactive dye or an acidic direct dye is used, the property of the chemical solution changes before the treatment. As a result, uneven processing and insufficient processing do not occur.

【0031】また、本発明によれば、投入槽内に、処理
液の旋回流により渦流を生じさせ、この渦流により投入
槽内を攪拌して粉体状薬剤を溶解,分散させる。そし
て、それによって得られた薬液を、処理液の噴射流によ
るエジェクタ作用でさらに溶解,分散させるようにして
いる。このように、上記2段階の溶解,分散を行うこと
により、粉体状薬剤を直接投入する方式において従来問
題視されていた溶解不良が起こらず、粉体状薬剤が充分
に溶解,分散されるようになる。このため、処理むらや
処理不足がなく、高品質の安定した処理を行うことがで
きるようになる。
Further, according to the present invention, a swirling flow of the treatment liquid is generated in the charging tank, and the powder is dissolved and dispersed by stirring the charging tank by the swirling flow. Then, the obtained chemical liquid is further dissolved and dispersed by an ejector action by the jet flow of the processing liquid. As described above, by performing the above-described two-stage dissolution and dispersion, poor dissolution, which has been conventionally regarded as a problem in the method of directly charging the powdered drug, does not occur, and the powdered drug is sufficiently dissolved and dispersed. Become like Therefore, high-quality stable processing can be performed without processing unevenness or processing shortage.

【0032】しかも、粉体状薬剤を一旦投入槽で溶解し
て薬液とし、その薬液をエジェクタ部において還流処理
液で希釈し、さらにそれを循環管路のポンプ吸込側に供
給して大量の循環処理液中に合流させることにより希釈
する。このように、粉体状薬剤を溶解した高濃度の薬液
を、所定の濃度に希釈した処理液として処理機に供給す
ることができる。このため、例えば、粉体状薬剤を循環
管路に直接投入した場合のように、部分的に極端に濃度
の高い薬液が循環して処理むらを引き起こすようなこと
もない。
In addition, the powdered drug is once dissolved in a charging tank to form a drug solution, and the drug solution is diluted with a reflux treatment liquid in an ejector section, and the diluted solution is supplied to a pump suction side of a circulation pipe to be circulated in a large amount. It is diluted by merging into the processing solution. As described above, a high-concentration chemical solution in which a powdery drug is dissolved can be supplied to a processing machine as a processing solution diluted to a predetermined concentration. For this reason, for example, unlike the case where the powdered drug is directly introduced into the circulation pipe, the extremely high concentration of the drug solution does not partially circulate, thereby causing processing unevenness.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施の形態例の粉体状薬剤の溶解供
給装置を示す説明図である。
FIG. 1 is an explanatory view showing an apparatus for dissolving and supplying a powdery medicine according to an embodiment of the present invention.

【図2】投入槽を示す断面図である。FIG. 2 is a sectional view showing a charging tank.

【図3】エジェクタ部を示す断面図である。FIG. 3 is a sectional view showing an ejector unit.

【図4】上記粉体状薬剤の溶解供給装置を液流式布帛処
理機に適用した例を示す説明図である。
FIG. 4 is an explanatory view showing an example in which the powdery drug dissolution supply device is applied to a liquid flow type cloth processing machine.

【図5】上記粉体状薬剤の溶解供給装置を気流式布帛処
理機に適用した例を示す説明図である。
FIG. 5 is an explanatory diagram showing an example in which the powdery drug dissolution supply device is applied to an airflow type cloth processing machine.

【図6】本発明の第2の実施の形態例の投入槽を示す断
面図である。
FIG. 6 is a cross-sectional view illustrating a charging tank according to a second embodiment of the present invention.

【図7】本発明の第3の実施の形態例のエジェクタ部を
示す断面図である。
FIG. 7 is a sectional view showing an ejector unit according to a third embodiment of the present invention.

【図8】本発明の第4の実施の形態例のエジェクタ部を
示す断面図である。
FIG. 8 is a sectional view showing an ejector unit according to a fourth embodiment of the present invention.

【図9】従来例の処理機を示す説明図である。FIG. 9 is an explanatory view showing a conventional processing machine.

【符号の説明】[Explanation of symbols]

1 投入槽 3 薬液供給配管 7 還流配管 10 循環管路 11 ポンプ DESCRIPTION OF SYMBOLS 1 Input tank 3 Chemical supply pipe 7 Reflux pipe 10 Circulation pipe 11 Pump

フロントページの続き (58)調査した分野(Int.Cl.6,DB名) D06B 23/00 B01F 1/00 D06B 3/24 D06B 23/20Continuation of the front page (58) Field surveyed (Int. Cl. 6 , DB name) D06B 23/00 B01F 1/00 D06B 3/24 D06B 23/20

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポンプを備えた外部循環管路を介して処
理液を循環することにより処理槽の繊維製品を加工処理
する方法において、密閉可能に構成された投入槽内に染
料,助剤等の粉体状薬剤を投入し、上記循環管路のポン
プ吐出側から処理液の一部を取り出して、この処理液を
旋回流として投入槽内に導入して上記粉体状薬剤を溶
解,分散させて薬液とし、この薬液を薬液供給配管を介
して上記循環管路のポンプ吸込側に希釈供給し、かつ、
上記循環管路のポンプ吐出側から処理液の一部を取り出
して上記薬液供給配管に還流させ、還流配管と薬液供給
配管との連通部において、還流処理液を薬液供給配管の
下流側に向かって噴射し、その噴射流によるエジェクタ
作用により、上流側の薬液を随伴吸引するとともに薬液
の溶解,分散を促進するようにしたことを特徴とする粉
体状薬剤の溶解供給方法。
1. A method for processing a textile product in a processing tank by circulating a processing liquid through an external circulation pipe provided with a pump, wherein a dye, an auxiliary agent, etc. are placed in a sealing tank. , And a part of the processing liquid is taken out from the pump discharge side of the circulation pipe, and the processing liquid is introduced into the charging tank as a swirling flow to dissolve and disperse the powdered medicine. To a chemical solution, diluting and supplying this chemical solution to the pump suction side of the circulation pipe via a chemical solution supply pipe, and
A part of the processing liquid is taken out from the pump discharge side of the circulation pipe and is returned to the chemical supply pipe, and at a communication portion between the reflux pipe and the chemical supply pipe, the reflux processing liquid is directed toward the downstream side of the chemical supply pipe. A method for dissolving and supplying a powdered drug, comprising ejecting and ejecting an upstream chemical solution with an ejector action by the jet flow, and promoting dissolution and dispersion of the chemical solution.
【請求項2】 処理液を旋回流として投入槽内に導入す
る際、導入処理液を2個所のノズルから右旋回流および
左旋回流として単独あるいは交互にもしくは同時に導入
する請求項1記載の粉体状薬剤の溶解供給方法。
2. The powder according to claim 1, wherein when the processing liquid is introduced into the charging tank as a swirling flow, the introduced processing liquid is introduced from two nozzles as a right swirling flow and a left swirling flow individually, alternately or simultaneously. For dissolving and supplying a drug in a liquid form.
【請求項3】 ポンプを備えた外部循環管路を介して処
理液を循環することにより処理槽の繊維製品を加工処理
する装置において、密閉可能に構成され染料,助剤等の
粉体状薬剤が投入される投入槽と、上記循環管路のポン
プ吐出側から分岐して上記投入槽へ連通する処理液導入
配管と、上記処理液導入配管と投入槽との連通部に設け
られ処理液を旋回流として導入させて投入槽内部の粉体
状薬剤を溶解,分散させる旋回流導入ノズルと、上記投
入槽から上記循環管路のポンプ吸込側に接続される薬液
供給配管とを備え、上記循環管路のポンプ吐出側から分
岐して上記薬液供給配管に延びる還流配管を設け、この
還流配管と薬液供給配管との連通部に、還流処理液を薬
液供給配管の下流側に向かって噴射してその噴射流によ
り上流側の薬液を随伴吸引するとともに薬液の溶解,分
散を促進するエジェクタ手段を設けたことを特徴とする
粉体状薬剤の溶解供給装置。
3. An apparatus for processing and treating textile products in a processing tank by circulating a processing liquid through an external circulation line provided with a pump, wherein the powdery chemicals such as dyes and auxiliaries are sealed. And a processing liquid introduction pipe branched from the pump discharge side of the circulation pipe and communicating with the charging tank, and a processing liquid provided in a communication portion between the processing liquid introduction pipe and the charging tank. A swirling flow introducing nozzle for introducing as a swirling flow to dissolve and disperse the powdery medicine in the charging tank; and a chemical liquid supply pipe connected from the charging tank to a pump suction side of the circulation pipeline, A reflux pipe branched from the pump discharge side of the pipeline and extending to the chemical supply pipe is provided, and a reflux treatment liquid is injected toward a downstream side of the chemical supply pipe at a communication portion between the reflux pipe and the chemical supply pipe. The jet stream causes the upstream chemical solution to flow An apparatus for dissolving and supplying a powdered drug, comprising ejector means for sucking and sucking and promoting dissolution and dispersion of the drug solution.
【請求項4】 旋回流導入ノズルとして、右旋回流導入
ノズルと左旋回流導入ノズルとの2個所のノズルが設け
られ、これらノズルからの導入処理液が、右旋回流およ
び左旋回流として交互にもしくは同時に投入槽に導入さ
れるようになっている請求項3記載の粉体状薬剤の溶解
供給装置。
4. A swirl flow introducing nozzle is provided with two nozzles of a right swirl flow introducing nozzle and a left swirl flow introducing nozzle, and the processing liquid introduced from these nozzles is alternately or right-rotated and left swirled. 4. The powdery drug dissolution supply device according to claim 3, wherein the powdery drug is supplied to the charging tank at the same time.
JP3970996A 1996-02-27 1996-02-27 Method for dissolving and supplying powdery drug and apparatus used therefor Expired - Fee Related JP2765817B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3970996A JP2765817B2 (en) 1996-02-27 1996-02-27 Method for dissolving and supplying powdery drug and apparatus used therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3970996A JP2765817B2 (en) 1996-02-27 1996-02-27 Method for dissolving and supplying powdery drug and apparatus used therefor

Publications (2)

Publication Number Publication Date
JPH09228231A JPH09228231A (en) 1997-09-02
JP2765817B2 true JP2765817B2 (en) 1998-06-18

Family

ID=12560530

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3970996A Expired - Fee Related JP2765817B2 (en) 1996-02-27 1996-02-27 Method for dissolving and supplying powdery drug and apparatus used therefor

Country Status (1)

Country Link
JP (1) JP2765817B2 (en)

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