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JPH09227838A - Apparatus for continuously forming stock paste by dissolution - Google Patents

Apparatus for continuously forming stock paste by dissolution

Info

Publication number
JPH09227838A
JPH09227838A JP7084196A JP7084196A JPH09227838A JP H09227838 A JPH09227838 A JP H09227838A JP 7084196 A JP7084196 A JP 7084196A JP 7084196 A JP7084196 A JP 7084196A JP H09227838 A JPH09227838 A JP H09227838A
Authority
JP
Japan
Prior art keywords
powder
water
paste
dissolver
pressure
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.)
Pending
Application number
JP7084196A
Other languages
Japanese (ja)
Inventor
Shoichi Sato
昌一 佐藤
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.)
KISHIMOTO KOSAKUSHO KK
Original Assignee
KISHIMOTO KOSAKUSHO KK
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 KISHIMOTO KOSAKUSHO KK filed Critical KISHIMOTO KOSAKUSHO KK
Priority to JP7084196A priority Critical patent/JPH09227838A/en
Publication of JPH09227838A publication Critical patent/JPH09227838A/en
Pending legal-status Critical Current

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  • Adhesives Or Adhesive Processes (AREA)
  • Treatment Of Fiber Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an apparatus by which a paste material such as a dyeing paste can be dissolved without deteriorating the paste as a result of the cleavage of molecules of the paste by the impellers and without forming any agglomerates of an unwetted powder even when the concentration of the solution is as high as 10-20%. SOLUTION: A specified amount of a powder material 1 being the starting material for a stock paste is discharged from a holding hopper 2, dusted with air blown from a blower 6 through a pressure feeder 5 and fed into a dissolution vessel 8. At the same time, water having a pressure which is always kept constant by a pressure regulation valve 11 is injected into the vessel at a controlled flow rate and sprayed over the dusted material 1 in the vessel 8 to dissolve the material 1 instantly without fail, and the obtained stock paste is transferred to a holding tank.

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、元糊の原料である
粉体材料を貯溜するホッパーより粉体を定量宛切出して
これを圧送器を介してブロワーより吹き出す空気により
粉塵化して溶解器内に送り込むと同時に、該溶解器の側
方より圧力調整弁により絶えず水圧を一定とし流量を制
御して注水して、この溶解器内において粉塵化した粉体
材料に所定の水圧による水を噴霧して粉体材料を瞬間的
にして確実に溶解して元糊の貯溜タンクへ移送する様に
した元糊自動連続溶解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 hopper for storing a powder material, which is a raw material for an original paste, in which a fixed amount of powder is cut out, and the powder is made into dust by air blown from a blower through a pressure feeder, and is melted in a dissolver At the same time, the water is constantly supplied from the side of the dissolver by a pressure regulating valve to keep the water pressure constant and the flow rate is controlled to inject water, and the powder material dusted in the dissolver is sprayed with water at a predetermined water pressure. The present invention relates to an automatic continuous paste dissolving device for a primary paste, which is capable of instantaneously and surely dissolving a powder material and transferring it to a storage tank for the original paste.

【0002】[0002]

【従来の技術】従来より各種の織物を染色する場合に用
いる糊液染料は、染剤と高粘度の元糊を配合したもので
あるが、この元糊を得る為には元糊の原料である澱粉質
または化学質の粉体を清水で溶解するもので、この粉体
を溶解するには内部に攪拌翼を設けた適当な大きさのタ
ンク内に粉体と清水とを適量宛投入しながら高粘度の元
糊に達するまで攪拌翼により広く攪拌して溶解している
ものである。しかしながら、粉体の保存期間中に往々に
して粉体の微粒子が湿気を吸い一部が顆粒状に固まって
いたり、或いは清水との攪拌に際して一部の粉体が清水
と溶解せず継粉(ママコ)状の固まりとなって容易に均
一な元糊が得られないものである。また、この攪拌タン
ク内での攪拌に際して手間を省かんとするため清水の注
水と共に多量粉体を一時に投入して長時間攪拌をしても
容易に均一にして高粘度の元糊が得られないものであ
る。
2. Description of the Related Art Conventionally, paste liquid dyes used for dyeing various kinds of fabrics are those in which a dye and a high-viscosity original paste are blended. In order to obtain the original paste, the original paste raw material is used. It dissolves a certain starchy or chemical powder with fresh water. To dissolve this powder, pour powder and fresh water into an appropriate amount in a tank of appropriate size with a stirring blade inside. However, the solution is agitated by a stirring blade to dissolve it until it reaches a high-viscosity original paste. However, during the storage period of the powder, fine particles of the powder often absorb moisture and partly solidify into granules, or when stirring with fresh water, some of the powder does not dissolve in fresh water and is sprinkled ( It becomes a mamako-like mass and it is not possible to easily obtain a uniform base paste. In addition, in order to save time and effort in stirring in this stirring tank, a large amount of powder is poured at a time together with the injection of fresh water, and even if the mixture is stirred for a long time, it is easily made uniform and a high-viscosity original paste is obtained. There is no such thing.

【0003】又、近時においては粉体を一定量宛て切り
出すと共に、これに空気を吹き付けて粉体を粉塵化させ
てたものを攪拌タンクに投入すると同時に清水を注入し
て攪拌翼により時間をかけて攪拌して、上記の如き継粉
(ママコ)状の固まりとならない様にしている場合もあ
るが、この場合における粉体と清水との投入量の関係は
粉体<清水であり、粉体の投入後所定の濃度まで清水を
注入して攪拌翼で均一化をはかっており、これらの粉体
の溶解濃度は2%以下で、多量の水に少量の粉体を投入
する為、比較的容易に溶解が可能であるが、反面攪拌翼
により糊の分子が剪断されて元糊としての性状が劣化す
ので、攪拌を伴わない粉体の溶解方法と、粉体の性状の
改良により粉体の溶解濃度が10乃至20%と多量に粉
体を投入しても均一なる元糊の製造方法が希求されてい
るものである。
Recently, a certain amount of powder is cut out and air is blown into the powder to make it into a stirring tank. At the same time, fresh water is injected and the stirring blades are used for time. In some cases, the mixture is stirred and stirred so that it does not form the above-mentioned powdered (Mamako) -like mass, but in this case, the relationship between the amount of powder and the amount of fresh water input is powder <fresh water, After pouring the body, fresh water is injected to a predetermined concentration to make it uniform with a stirring blade. The dissolved concentration of these powders is 2% or less, and a small amount of powder is poured into a large amount of water. Although it is possible to easily dissolve it, on the other hand, since the glue molecules are sheared by the stirring blades and the properties as the original paste are deteriorated, the method of dissolving the powder without stirring and improving the properties of the powder Even if a large amount of powder is added, the dissolved concentration of the body is 10 to 20%. Method for producing a source glue made in which is desired.

【0004】[0004]

【発明が解決しようとする課題】本発明はかかる現状に
鑑みて創作したものであって、その解決しょうとする課
題は、染色糊等の糊材料を溶解する場合、攪拌翼の攪拌
により糊分子が剪断されて劣化を生じせしめることなく
溶解すると共に、溶解濃度を10乃至20%に向上させ
ても継粉(ママコ)状の固まりとならない様に均一に溶
解が可能にせんとするものである。
SUMMARY OF THE INVENTION The present invention was created in view of the present situation, and the problem to be solved is to dissolve a glue material such as a dye paste by stirring a glue molecule by stirring with a stirring blade. Dissolves without causing shearing and deterioration, and even if the dissolution concentration is increased to 10 to 20%, it is possible to dissolve uniformly so that it does not form a lump like powder (Mamako). .

【0005】[0005]

【課題を解決するための手段】本発明は、元糊の原料で
ある粉体材料を貯溜するホッパーの下端よりスクリュー
フィーダー等の公知の切り出し手段により粉体を定量宛
切出してこれを圧送器に移送すると共に、圧送器の他方
よりはブロワーの吹き出す空気によりこの粉体を粉塵化
してこれに連続する溶解器内に送り込む様にし、更に該
溶解器の側方上端よりは流量計、圧力スイッチ、圧力調
節弁及び電磁弁を介した通水管を配管して、絶えず水圧
を一定とし流量を制御して注水して、この溶解器内にお
いて粉塵化した粉体材料に所定の水圧による水を噴霧し
て粉体材料を瞬間的にして確実に溶解して元糊の貯溜タ
ンクへ移送する様にしているものである。
According to the present invention, the powder is quantitatively cut out by a known cutting means such as a screw feeder from a lower end of a hopper for storing the powder material which is a raw material of the original paste, and the powder is fed to a pressure feeder. Along with the transfer, the powder is made into dust by the air blown from the blower from the other side of the pressure feeder and fed into the continuous melter, and further from the side upper end of the melter, a flow meter, a pressure switch, Water pipes through the pressure control valve and solenoid valve are laid to keep the water pressure constant and the flow rate is controlled to inject water, and the powder material dusted in this dissolver is sprayed with water at a predetermined water pressure. The powder material is instantaneously and surely melted and transferred to the storage tank for the original paste.

【0006】[0006]

【発明の実施の形態】本発明によれば、粉体材料を貯溜
するホッパーの下端よりスクリューフィーダー等の公知
の切り出し手段により粉体を定量宛切出すに際して、そ
の回転数を制御することにより粉体の単位時間当りの粉
体の送出量を割り出して、これをブロワーの吹き出す空
気により粉塵化してこれに連続する溶解器内に送り込む
ものであり、該溶解器の側方に配管する通水管には流量
計、圧力スイッチ、圧力調節弁及び電磁弁を介して、給
水量の測定と共に水の噴射圧力を調整して前記粉体の投
入量に対して単位時間当りの給水量を測定するものであ
る。更に、この溶解器には、その中央の上方より圧送器
より粉塵化された粉体を導入すると共に、側方上端の通
水管より導入した水は、仕切板の下周面に楕円形にして
縦断面を逆円錐形の噴出孔を適宜数の開口すると共にそ
の下面より噴出孔の中心に向け逆V形の噴霧溝を削成し
て、これに導入された水は溶解器周面の全体に噴霧され
る様にすると共に、この溶解器の中程において粉体と噴
霧水とが接触する箇所に括れを設けて粉体と噴霧水を強
制的に接触させて粉体材料を瞬間的にして確実に溶解を
促進させて上記の課題を達成せんとしているものであ
る。
According to the present invention, when the powder is quantitatively cut from a lower end of a hopper for storing the powder material by a known cutting means such as a screw feeder, the number of revolutions of the powder is controlled to control the powder. The amount of powder to be delivered per unit time of the body is calculated, and this is made into dust by the air blown out by the blower and sent into the continuous melter, and to the water pipe that is piped to the side of the melter. Is to measure the amount of water supply through a flow meter, pressure switch, pressure control valve and solenoid valve, and to adjust the water injection pressure and to measure the amount of water supply per unit time for the amount of powder added. is there. Furthermore, the powder that was dusted from the pressure feeder was introduced from above the center of the dissolver, and the water introduced from the water pipe at the upper end of the side was made into an elliptical shape on the lower peripheral surface of the partition plate. The vertical cross section has an appropriate number of reverse conical ejection holes, and the reverse V-shaped spray groove is cut from the lower surface toward the center of the ejection holes, and the water introduced into this is the entire peripheral surface of the dissolver. The powder material is instantly sprayed by forcing the powder and spray water to come into contact with each other in the middle of the dissolver. Therefore, it is intended to surely promote the dissolution and achieve the above-mentioned problems.

【0007】[0007]

【実施例】本発明の一実施例を図面に基づき説明すれ
ば、元糊の原料である粉体材料1を貯溜するホッパー2
の下端よりスクリューフィーダー等の公知の切り出し手
段3により粉体を定量宛切出すに際して、その可変速モ
ーター4の回転数を制御することにより粉体の単位時間
当りの粉体の送出量を割り出して圧送器5に移送すると
共に、圧送器5の他方よりはブロワー6の吹き出す空気
によりこの粉体を粉塵化したものを送粉管7により連続
する溶解器8内の中央上方より送り込む様にし、更に該
溶解器8の側方上端よりは流量計9、圧力スイッチ1
0、圧力調節弁11及び電磁弁12を介した通水管13
を配管して、給水量の測定と共に水の噴射圧力を調整し
て前記粉体の投入量に対して単位時間当りの給水量を測
定しつつ、所定の最低圧力以下に水圧が低下した場合に
は装置全体を停止せしめる様にして元糊の濃度を維持す
る様にしているものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the present invention will be described with reference to the drawings. A hopper 2 for storing a powder material 1 which is a raw material for an original paste.
When the powder is quantitatively cut out from the lower end of the powder by a known cutting means 3 such as a screw feeder, the rotation amount of the variable speed motor 4 is controlled to determine the amount of the powder delivered per unit time. The powder is made to be dust by the air blown from the blower 6 from the other side of the pressure feeder 5, and the powdered tube 7 is fed from above the center of the continuous melter 8 by the powder feeding pipe 7. From the lateral upper end of the dissolver 8, a flow meter 9, a pressure switch 1
0, water passage pipe 13 via pressure control valve 11 and solenoid valve 12
When measuring the amount of water supply and adjusting the water injection pressure and measuring the amount of water supply per unit time with respect to the amount of powder input, when the water pressure drops below a predetermined minimum pressure. Is to keep the concentration of the original paste by stopping the entire device.

【0008】更に、この溶解器8の中央上方に接続する
送粉管7は圧送器5より粉塵化された粉体を導入すると
共に、この側方上端に配管する通水管13より導入した
水は、下面を仕切板14により区画された中央に、楕円
形にして縦断面を逆円錐形の噴出孔15を適宜数の開口
すると共に、その下面より噴出孔15の中心に向け逆V
形の噴霧溝16を削成して、これに導入された水は噴出
孔15より溶解器8の内周面の全体に噴霧され且つ、こ
の溶解器8の中程において粉体18と噴霧水19とが接
触する箇所に括れ17を設けてこれらを強制的に接触さ
せて粉体材料を瞬間的にして確実に溶解を促進して溶解
液受け20より吐出ポンプ21より図示しない元糊の貯
溜タンクへ移送する様にしているものである。
Further, the powder feeding pipe 7 connected to the upper center of the dissolver 8 introduces the powdered dust from the pressure feeder 5, and the water introduced from the water pipe 13 piped to the upper end of the side is In the center divided by the partition plate 14, an ejection hole 15 having an elliptical shape and a vertical cross section of an inverted conical shape is opened in an appropriate number, and an inverted V is formed from the lower surface toward the center of the ejection hole 15.
The water introduced into the spray groove 16 having a shape of a square shape is sprayed from the ejection hole 15 to the entire inner peripheral surface of the dissolver 8, and in the middle of the dissolver 8, the powder 18 and the spray water are sprayed. A constriction 17 is provided at a position where it comes into contact with 19, and these are forcibly brought into contact with each other to instantaneously and surely promote the dissolution of the powder material, and the dissolution liquid receiver 20 discharges the pump 21 to store the original paste (not shown). It is designed to be transferred to a tank.

【0009】本発明による粉体材料1を貯溜するポッパ
ー2の下端より切り出すスクリューフィーダー等の公知
の切り出し手段3によれば、これを回転させる可変速モ
ーター4の回転数を制御することにより粉体の単位時間
当りの送出量が決定出来ると共に、これをエジェクタ方
式の圧送器5に移送して他方のブロアー6より吹き出す
空気により粉体を粉塵化して送粉管7で溶解器8内の中
央上方より送り込む様にしているものである。
According to the known cutting means 3 such as a screw feeder for cutting the powder material 1 from the lower end of the popper 2 for storing the powder material 1, the powder is controlled by controlling the rotation speed of the variable speed motor 4 for rotating the powder material 1. Can be determined per unit time, and this is transferred to the ejector type pressure feeder 5 and the air blown from the other blower 6 atomizes the powder, and the powder transfer pipe 7 is used to move the upper part of the inside of the dissolver 8 to the upper center. I try to send more.

【0010】また、溶解器8の側方上端に配管する通水
管13より導入した水は、仕切板14の中央に楕円形に
して縦断面を逆円錐形として適宜数開口した噴出孔15
と、その下面より逆V字形に削成した噴霧溝16により
水滴とならず噴出孔15より溶解器8の内周面の全体に
噴霧され、更にこの溶解器8の中程において粉体18と
噴霧水19とが接触する箇所に括れ17を設けて周壁よ
りの噴霧水19を粉体18が最も多く通過する中心部に
集めてこれらを強制的に接触させて粉体材料を瞬間的に
して確実に溶解を促進させる様にしているものである。
The water introduced from the water passage 13 which is provided at the lateral upper end of the dissolver 8 has an elliptical shape in the center of the partition plate 14 and has a vertical cross section of an inverted conical shape.
Then, the spray groove 16 cut from the lower surface thereof in an inverted V shape does not form water droplets and is sprayed from the ejection hole 15 onto the entire inner peripheral surface of the dissolver 8. A constriction 17 is provided at a position where the sprayed water 19 comes into contact, and the sprayed water 19 from the peripheral wall is collected in the central portion where the powder 18 passes most, and these are forcibly contacted to instantly make the powder material. It is intended to surely promote the dissolution.

【0011】[0011]

【発明の効果】本発明は、粉体材料1を貯溜するホッパ
ー2より単位時間当りの粉体を定量宛切出すと共に、こ
れをブロワー6の吹き出す空気により粉塵化してこれに
連続する溶解器8内に送り込み、他方この側方に配管す
る通水管13には流量計9、圧力スイッチ10、圧力調
節弁11等を介して、給水量の測定と共に水の噴射圧力
を調整して前記粉体の投入量に対して単位時間当りの給
水量を測定して所定の元糊濃度を維持する様にし、ま
た、粉塵化した粉体と水を導入する溶解器8には、下面
を仕切板14により区画された中央に、楕円形にして縦
断面を逆円錐形の噴出孔15を適宜数の開口すると共
に、その下面より噴出孔15の中心に向け逆V形の噴霧
溝16を削成しているので、これに導入された水は水滴
とならずに確実に溶解器周面の全体に噴霧されると共
に、この溶解器の中程において粉体18と噴霧水19と
が接触する箇所に括れ17を設けてこれらを強制的に接
触させて粉体材料を瞬間的にして確実に溶解を促進させ
るものであるから、従来の如く攪拌翼の攪拌により糊分
子が剪断されて劣化を生じせしめることなく溶解させる
と共に、溶解濃度を10乃至20%に向上させても継粉
(ママコ)状の固まりとならない様に均一に溶解が可能
した極めて有用なるものである。
According to the present invention, the powder per unit time is cut out in a fixed amount from the hopper 2 which stores the powder material 1, and this is made into dust by the air blown out from the blower 6, and the dissolver 8 is connected to this. Into the water pipe 13 which is fed into the inside of the pipe, and on the other hand, through the flow meter 9, the pressure switch 10, the pressure control valve 11 and the like, the water supply amount is measured and the water injection pressure is adjusted to The water supply amount per unit time is measured with respect to the input amount so that a predetermined original paste concentration is maintained, and the lower surface of the dissolver 8 for introducing dusted powder and water is separated by a partition plate 14. An appropriate number of ejection holes 15 each having an elliptical shape and a vertical conical cross section are opened in the divided center, and an inverse V-shaped spray groove 16 is formed from the lower surface thereof toward the center of the ejection holes 15. The water introduced into this is dissolved without forming drops. The powder material is sprayed over the entire peripheral surface, and a constriction 17 is provided at a position where the powder 18 and the spray water 19 come into contact with each other in the middle of the dissolver to force them to come into contact with each other to instantaneously change the powder material. Therefore, it is possible to surely promote the dissolution, so that the paste molecules are not sheared and deteriorated by the stirring of the stirring blade as in the conventional case, and even if the dissolution concentration is improved to 10 to 20%. It is extremely useful because it can be uniformly dissolved so that it does not form a (mamako) lump.

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

【図1】本発明の一実施例の構成全体を示す概略フロー
図である。
FIG. 1 is a schematic flowchart showing the overall configuration of an embodiment of the present invention.

【図2】溶解器の縦断切断面図である。FIG. 2 is a vertical cross-sectional view of the dissolver.

【図3】図2A−Aにおける切断面図である。FIG. 3 is a sectional view of FIG. 2A-A.

【図4】噴出孔の一部拡大底面図である。FIG. 4 is a partially enlarged bottom view of ejection holes.

【図5】図4B−Bにおける切断面図である。FIG. 5 is a cross-sectional view of FIG. 4B-B.

【符号の説明】[Explanation of symbols]

1 粉体材料 2 ホッパー 3 切り出し手段 4 可変速モーター 5 圧送器 6 ブロワー 7 送粉管 8 溶解器 9 流量計 10 圧力スイッチ 11 圧力調節弁 12 電磁弁 13 通水管 14 仕切板 15 噴出孔 16 噴霧溝 17 括れ 18 粉体 19 噴霧水 20 溶解液受け 21 吐出ポンプ DESCRIPTION OF SYMBOLS 1 Powder material 2 Hopper 3 Cutting means 4 Variable speed motor 5 Pressure feeder 6 Blower 7 Powder feeder 8 Melting device 9 Flowmeter 10 Pressure switch 11 Pressure control valve 12 Electromagnetic valve 13 Water passage pipe 14 Partition plate 15 Spray hole 16 Spray groove 17 Constriction 18 Powder 19 Spray water 20 Dissolution liquid receiver 21 Discharge pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 粉体材料を貯溜するホッパーの下端より
単位時間当りの粉体を切り出し手段を設けてこれを圧送
器に移送すると共に、圧送器の他方より吹き出す空気に
よりこの粉体を粉塵化して送粉管により溶解器内に送り
込む様にし、更に該溶解器には所定の計器を配設した通
水管を配管して、給水量と水圧等を検知して前記粉体の
投入量に対応して導入した水は、下面を仕切板により区
画された中央に、楕円形にして縦断面を逆円錐形の噴出
孔を適宜数の開口すると共に、その下面より噴出孔の中
心に向け逆V形の噴霧溝を削成して、これに導入された
水は噴出孔より溶解器の内周面の全体に噴霧され且つ、
この溶解器の中程において粉体と噴霧水とが接触する箇
所に括れを設けてこれらを強制的に接触させて粉体材料
を瞬間的にして確実に溶解することを特徴とする元糊自
動連続溶解装置。
1. A means for cutting out powder per unit time from the lower end of a hopper for storing powder material is provided to transfer the powder to a pressure feeder, and at the same time, air blown from the other side of the pressure feeder atomizes the powder. To feed into the dissolver through a powder feeding pipe, and to the dissolver, a water pipe with a specified instrument is installed to detect the amount of water supplied and the water pressure and respond to the amount of powder added. The water introduced in this way has an appropriate number of ejection holes with an elliptical shape and an inverted conical longitudinal section opened in the center where the lower surface is divided by a partition plate, and the reverse V is directed from the lower surface toward the center of the ejection hole. Water is introduced into this by shaving a spray groove in the shape of
An original paste automatic that is characterized in that a constriction is provided in the middle of the dissolver where the powder and the spray water come into contact with each other to forcefully contact them and the powder material is instantaneously and surely dissolved. Continuous melting device.
JP7084196A 1996-02-19 1996-02-19 Apparatus for continuously forming stock paste by dissolution Pending JPH09227838A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7084196A JPH09227838A (en) 1996-02-19 1996-02-19 Apparatus for continuously forming stock paste by dissolution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7084196A JPH09227838A (en) 1996-02-19 1996-02-19 Apparatus for continuously forming stock paste by dissolution

Publications (1)

Publication Number Publication Date
JPH09227838A true JPH09227838A (en) 1997-09-02

Family

ID=13443202

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7084196A Pending JPH09227838A (en) 1996-02-19 1996-02-19 Apparatus for continuously forming stock paste by dissolution

Country Status (1)

Country Link
JP (1) JPH09227838A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100817512B1 (en) * 2007-11-16 2008-03-27 (주)동일캔바스엔지니어링 Powder particle mixing unit and powder particle dissolving apparatus using the same
JP2012200722A (en) * 2011-03-28 2012-10-22 Izumi Food Machinery Co Ltd Powder dissolving apparatus
JP2014518343A (en) * 2011-06-28 2014-07-28 アッリゥ グロウプ オイ Method for exhausting transport air from a mixture of compressed air and binder
WO2018042486A1 (en) * 2016-08-29 2018-03-08 株式会社日阪製作所 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus
CN114082313A (en) * 2021-12-08 2022-02-25 碟石环保设备河北有限公司 A kind of PAM medicinal liquid preparation method and control system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100817512B1 (en) * 2007-11-16 2008-03-27 (주)동일캔바스엔지니어링 Powder particle mixing unit and powder particle dissolving apparatus using the same
JP2012200722A (en) * 2011-03-28 2012-10-22 Izumi Food Machinery Co Ltd Powder dissolving apparatus
JP2014518343A (en) * 2011-06-28 2014-07-28 アッリゥ グロウプ オイ Method for exhausting transport air from a mixture of compressed air and binder
WO2018042486A1 (en) * 2016-08-29 2018-03-08 株式会社日阪製作所 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus
CN114082313A (en) * 2021-12-08 2022-02-25 碟石环保设备河北有限公司 A kind of PAM medicinal liquid preparation method and control system

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