WO2018042486A1 - Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus - Google Patents

Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus Download PDF

Info

Publication number
WO2018042486A1
WO2018042486A1 PCT/JP2016/075179 JP2016075179W WO2018042486A1 WO 2018042486 A1 WO2018042486 A1 WO 2018042486A1 JP 2016075179 W JP2016075179 W JP 2016075179W WO 2018042486 A1 WO2018042486 A1 WO 2018042486A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
flow path
section
treatment agent
type fabric
Prior art date
Application number
PCT/JP2016/075179
Other languages
French (fr)
Japanese (ja)
Inventor
高橋 正志
清水 徹
壮 本間
英夫 柄崎
成治 伊藤
Original Assignee
株式会社日阪製作所
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 株式会社日阪製作所 filed Critical 株式会社日阪製作所
Priority to PCT/JP2016/075179 priority Critical patent/WO2018042486A1/en
Priority to KR1020197005729A priority patent/KR102503513B1/en
Priority to JP2018536373A priority patent/JP6843145B2/en
Priority to CN201680088832.0A priority patent/CN109661489B/en
Publication of WO2018042486A1 publication Critical patent/WO2018042486A1/en

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B23/00Component parts, details, or accessories of apparatus or machines, specially adapted for the treating of textile materials, not restricted to a particular kind of apparatus, provided for in groups D06B1/00 - D06B21/00
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B23/00Component parts, details, or accessories of apparatus or machines, specially adapted for the treating of textile materials, not restricted to a particular kind of apparatus, provided for in groups D06B1/00 - D06B21/00
    • D06B23/20Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation
    • D06B23/205Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation for adding or mixing constituents of the treating material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F21/00Dissolving
    • B01F21/30Workflow diagrams or layout of plants, e.g. flow charts; Details of workflow diagrams or layout of plants, e.g. controlling means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids

Definitions

  • the present invention relates to a treatment agent dissolving device for a fluid flow type fabric treatment device for supplying a treatment agent for fabric treatment to a fluid flow type fabric treatment device for treating the fabric, and a fluid flow type fabric treatment device.
  • Patent Document 1 As one of fabric processing apparatuses for processing fabrics, there is known a liquid flow type fabric processing apparatus that circulates a liquid used for dyeing and processes the fabric. Conventionally, a treatment agent dissolving apparatus for a liquid flow type fabric processing apparatus for supplying a treatment agent for fabric treatment to the liquid flow type fabric treatment apparatus has been provided (Patent Document 1).
  • the treatment agent dissolving apparatus 9100 is connected to a liquid flow type fabric treatment apparatus 9000 provided with a circulation system 9130 through which a liquid used for dyeing circulates.
  • the processing agent dissolving apparatus 9100 includes a supply tank 9120 in which an input port 9110 into which the processing agent W is input is formed, and the supply tank 9120 is directly connected to the circulation system 9130.
  • the supply tank 9120 supplies the processing agent W to the liquid used for dyeing that circulates in the circulation system 9130 when the processing agent W is input from the input port 9110.
  • the usage amount of the processing agent W is determined based on the amount of the fabric to be processed and the amount of liquid used for dyeing, and when the fabric is processed in an amount smaller than the determined amount, The fabric may not be properly processed. Therefore, it is desired that substantially the entire amount of the processing agent W is dispersed or dissolved in the liquid used for dyeing circulating in the liquid flow type fabric processing device 9000 without losing the pre-measured processing agent W. It is also desirable that the agent W be reliably dispersed or dissolved in the liquid.
  • the supply tank 9120 is directly fixed to the upper part of the pipe 9140 constituting the circulation system 9130, and the processing agent W is circulated from the input port 9110 positioned above the pipe 9140.
  • the processing agent W is circulated from the input port 9110 positioned above the pipe 9140.
  • the treatment agent dissolving apparatus 9100 since there is no mechanism for sufficiently dispersing or dissolving the treatment agent W with respect to the liquid used for dyeing, the treatment agent W is not sufficiently dispersed or dissolved, but is dispersed or dissolved. In some cases, no treatment agent directly contacts the fabric. This may cause processing unevenness and fabric stains.
  • the present invention provides a treatment agent dissolving apparatus for a liquid flow type fabric treatment apparatus and a liquid flow type cloth treatment apparatus capable of sufficiently dispersing or dissolving the treatment agent in a liquid used for dyeing.
  • the task is to do.
  • the treatment agent dissolving apparatus for the liquid flow type fabric treatment apparatus is in the form of powder and the treatment agent for treating the fabric is supplied from one end, and the other end is connected to the circulation system through which the liquid used for dyeing circulates.
  • the flow path includes a first section and a second section located on the one end side with respect to the first section, and the cross-sectional area of the first section is equal to the flow path of the second section. It is smaller than a cross-sectional area, and the ejection unit may eject the liquid used for the staining toward the first section.
  • the flow path has a third section located on the other end side with respect to the first section, and the flow path cross-sectional area of the third section is larger than the flow path cross-sectional area of the first section. May be.
  • the main body may have an inner peripheral surface that defines the flow path, and may include a liquid supply unit that supplies the liquid used for the staining along the inner peripheral surface.
  • the liquid supply unit may supply the liquid used for the staining in the circumferential direction of the inner peripheral surface.
  • the main body may have an inner peripheral surface that divides the flow path, and the ejection unit may eject the liquid used for the staining from the inner peripheral surface into the flow path.
  • the ejection unit may eject the liquid used for the staining into the flow path from a plurality of positions spaced in the circumferential direction on the inner peripheral surface.
  • a first dispersion member provided at the other end of the flow path and having a plurality of openings may be provided.
  • a second dispersion member having a plurality of openings is provided so as to overlap the first dispersion member in the flow direction of the flow path, and the second dispersion member includes a plurality of openings of the second dispersion member and the first dispersion member. You may arrange
  • a liquid flow type fabric treatment apparatus circulates the treatment agent dissolving device, a supply member for supplying a powdery treatment agent toward the one end of the flow path, and a liquid used for the dyeing. And a circulation system for treating the fabric and supplying the liquid used for the dyeing from the other end of the flow path.
  • FIG. 1 is a flowchart for explaining a liquid flow type fabric treatment apparatus including a treatment agent dissolving apparatus according to a first embodiment of the present invention.
  • FIG. 2 is an external view of the treatment agent dissolving apparatus according to the embodiment.
  • FIG. 3 is a cross-sectional view of the treatment agent dissolving apparatus according to the embodiment, and is a cross-sectional view taken along the line III-III in FIG.
  • FIG. 4 is a cross-sectional view of the treatment agent dissolving apparatus according to the second embodiment of the present invention.
  • FIG. 5 is a flowchart for explaining a liquid flow type fabric processing apparatus provided with a conventional processing agent dissolving apparatus.
  • FIG. 6 is a schematic diagram for explaining a method of supplying a treatment agent to a circulation system in a conventional treatment agent dissolving apparatus.
  • processing apparatus 100 liquid flow type fabric processing apparatus 100 according to the first embodiment of the present invention
  • dissolving apparatus 1 processing agent dissolving apparatus 1
  • the fabric is processed with a liquid used for dyeing.
  • the liquid used for dyeing includes a liquid in a state where a processing agent for processing a fabric (processing agent for processing the fabric) is mixed.
  • staining contains the liquid etc. in which a processing agent is not mixed.
  • the treating agent for fabric treatment is a dye for dyeing.
  • This treatment agent includes an auxiliary agent (for example, sodium sulfate (sodium sulfate)) used for the purpose of promoting dyeing of the fabric, a treatment agent for flameproofing, and the like, if necessary.
  • the treatment agent of this embodiment is a powdery treatment agent.
  • the processing apparatus 100 circulates a liquid used for dyeing (hereinafter simply referred to as “liquid”) and circulates a fabric, a supply system 11 for supplying a powdery processing agent, and a supply member 11. And a dissolving device 1 for supplying a liquid to the circulation system 10.
  • liquid used for dyeing
  • the circulation system 10 includes a retention tank 101 for treating the fabric, a transfer pipe 102 that forms the liquid circulation system 10 together with the retention tank 101, a circulation pump 103 that circulates the liquid between the retention tank 101 and the transfer pipe 102, Is provided.
  • the staying tank 101 has a main body portion 1011 serving as a region for processing the fabric, an inlet portion 1012 for introducing the liquid into the main body portion 1011, and an outlet portion 1013 for sending the liquid flowing out from the main body portion 1011 to the transfer pipe 102. .
  • the transfer pipe 102 is connected to the first transfer pipe 1021 that connects the outlet 1013 of the retention tank 101 and the suction part 1031 of the circulation pump 103, and the second transfer that connects the discharge part 1032 of the circulation pump 103 and the inlet 1012 of the retention tank 101.
  • the liquid is pressurized by the circulation pump 103. Therefore, in the present embodiment, the pressure in the second transfer pipe 1022 is higher than the pressure in the first transfer pipe 1021.
  • the liquid is discharged from the discharge portion 1032 of the circulation pump 103 and returns to the retention tank 101 via the inlet portion 1012, and then passes through the outlet portion 1013 of the retention tank 101 and the first transfer pipe 1021 while processing the fabric. Return to the suction portion 1031 of the circulation pump 103.
  • the liquid circulates.
  • the circulation pump 103 has a suction part 1031 for sucking liquid and a discharge part 1032 for sending liquid.
  • Transfer pipes 104 and 105 are branched from the circulation system 10.
  • the transfer pipes 104 and 105 merge at the transfer pipe 106.
  • the transfer pipe 106 and the transfer pipe 107 branched from the transfer pipe 106 are connected to the upstream side of the dissolving apparatus 1, and the liquid is supplied to the dissolving apparatus 1 from the transfer pipes 106 and 107.
  • a transfer pipe 108 is branched from the circulation system 10.
  • the transfer pipe 108 is connected to the downstream side of the dissolving apparatus 1, and the liquid is supplied from the dissolving apparatus 1 to the circulation system 10 through the transfer pipe 108.
  • the supply member 11 stores the processing agent supplied from one end and supplies the stored processing agent to the dissolution apparatus 1 from the other end.
  • the supply member 11 of this embodiment is a so-called hopper.
  • the other end portion of such a hopper is, for example, a cylindrical shape whose diameter is reduced toward the other end.
  • the melting device 1 includes a main body 4 having an inner peripheral surface 3 that defines a flow path 2 and an injection unit 5 that injects liquid into the flow path 2.
  • the main body 4 of the present embodiment includes a dissolving portion 40 that disperses or dissolves the treatment agent in the liquid, and a connecting portion 41 that connects the supply member 11 and the dissolving portion 40.
  • the melting part 40 and the connecting part 41 in the main body 4 are integrally formed.
  • the supply member 11 is connected to one end 410 (the upper end in FIGS. 2 and 3) of the connecting portion 41.
  • the dissolution apparatus 1 of the present embodiment includes a liquid supply unit 7 that supplies a liquid along the inner peripheral surface 3. Furthermore, the dissolution apparatus 1 of the present embodiment includes a dispersion unit 8 that is connected to the flow path 2 and disperses the treatment agent remaining undissolved in the liquid pushed out from the flow path 2.
  • a liquid supply unit 7 that supplies a liquid along the inner peripheral surface 3.
  • the dissolution apparatus 1 of the present embodiment includes a dispersion unit 8 that is connected to the flow path 2 and disperses the treatment agent remaining undissolved in the liquid pushed out from the flow path 2.
  • the flow path 2 is a space surrounded by the inner peripheral surface 3.
  • the shape of the flow path 2 will be described, but this description will explain the shape of the inner peripheral surface 3 that defines the flow path 2 having the following shape.
  • the powdery processing agent is supplied from the supply member 11 from one end 20 (the upper end in FIG. 3) of the flow path 2. Furthermore, the other end 21 (the lower end in FIG. 3) of the flow path 2 is connected to the main body portion 1011 of the staying tank 101 via the transfer pipe 108 to supply the liquid to the circulation system 10.
  • the cross section of the flow path 2 of the present embodiment is, for example, circular.
  • the “cross section of the flow path 2” refers to a cross section in a direction perpendicular to the central axis ⁇ of the flow path 2.
  • the flow path 2 of the present embodiment includes the first section 22, the second section 23 located on the one end 20 side of the first section 22, and the other end 21 side of the first section 22 in the dissolving section 40.
  • a third section 24 located at In the melting part 40, the second section 23, the first section 22, and the third section 24 are positioned in order from the one end 20 to the other end 21 of the flow path 2.
  • the flow path cross-sectional area of the first section 22 is smaller than that of the second section 23.
  • the cross-sectional area of the third section 24 is larger than the cross-sectional area of the first section 22. That is, the cross-sectional area of the first section 22 located between the one end 20 side and the other end 21 side is the second section 23 located on the one end 20 side and the third section 24 located on the other end 21 side. It is smaller than the cross-sectional area of the channel.
  • the second section 23 includes a first region 231 located on the one end 20 side, a second region 232 located between the one end 20 side and the other end 21 side, and a third region 233 located on the other end 21 side.
  • a first region 231, a second region 232, and a third region 233 are sequentially connected from one end 20 to the other end 21 of the flow path 2.
  • the channel cross-sectional area of the first region 231 decreases as it approaches the other end 21 side. That is, the diameter of the first region 231 decreases toward the other end 21 side.
  • the inclination angle of the first region 231 (between the portion defining the first region 231 on the inner peripheral surface 3 and the direction perpendicular to the central axis ⁇ of the flow path 2 (horizontal direction in FIG. 3)).
  • the angle ⁇ 1) is larger than the angle of repose of the powdery treatment agent.
  • the powdery treatment agent slides down the portion defining the first region 231 on the inner peripheral surface 3. Cheap.
  • the inclination angle of the second region 232 (the angle ⁇ 2 between the portion defining the second region 232 on the inner peripheral surface 3 and the direction orthogonal to the central axis ⁇ of the flow channel 2 (horizontal direction in FIG. 3)) It is larger than the angle of repose of the powdery treatment agent. Therefore, for the same reason as in the first region 231, the powdery treatment agent easily slides down the portion defining the second region 232 on the inner peripheral surface 3.
  • (theta) 2 is larger than the angle of repose of a powdery processing agent, and is 90 degrees or less.
  • the second region 232 is provided with an injection hole for injecting liquid into the flow path 2.
  • the flow path cross-sectional area of the third region 233 decreases as it approaches the other end 21. That is, the diameter of the third region 233 decreases as it approaches the other end 21 side.
  • the inclination angle of the third region 233 (between the portion defining the third region 233 on the inner peripheral surface 3 and the direction perpendicular to the central axis ⁇ of the flow path 2 (horizontal direction in FIG. 3)).
  • the angle ⁇ 3) is larger than the angle of repose of the powdery treatment agent. Therefore, for the same reason as in the first region 231, the powdery treatment agent easily slides down the portion that partitions the third region 233 on the inner peripheral surface 3.
  • the cross-sectional area of the second section 22 is the smallest.
  • the third section 24 has a first region 241 located on the one end 20 side and a second region 242 located on the other end 21 side.
  • the flow path cross-sectional area of the first region 241 increases as it approaches the other end 21 side. That is, the diameter of the first region 241 increases as it approaches the other end 21 side.
  • the flow path cross-sectional area of the second region 242 increases as it approaches the other end 21 side. That is, the diameter of the second region 242 increases as it approaches the other end 21 side.
  • the inclination angle of the second region 242 (the angle ⁇ 5 between the portion defining the second region 242 on the inner peripheral surface 3 and the direction perpendicular to the central axis ⁇ of the flow path 2 (horizontal direction in FIG. 3)) Is the inclination angle of the first region 241 (the angle ⁇ 4 between the portion defining the first region 241 on the inner peripheral surface 3 and the direction perpendicular to the central axis ⁇ of the flow path 2 (horizontal direction in FIG. 3)) Bigger than.
  • the powdery processing agent supplied from the one end 20 does not move in the horizontal direction (the horizontal direction in FIG. 3) in the flow path 2, It moves linearly in the direction from the one end 20 toward the other end 21.
  • the injection unit 5 is connected to the upstream part of the circulation system 10 than the part to which the other end 21 is connected. Liquid is supplied from the circulation system 10 to the injection unit 5 of the present embodiment via the transfer pipe 106 (see FIG. 1).
  • the injection unit 5 of the present embodiment injects liquid from the inner peripheral surface 3 into the flow path 2 as described above.
  • the ejection unit 5 ejects the liquid into the flow path 2 from a plurality of positions (four injection holes in the present embodiment) spaced in the circumferential direction on the inner peripheral surface 3.
  • the four injection holes are provided at equal intervals in the circumferential direction.
  • each of the four injection holes is provided at a distance equal to the other end 21 of the flow path 2.
  • the injection unit 5 of the present embodiment includes a first portion 50 composed of a plurality of flow paths (four flow paths in the present embodiment) respectively communicating with a plurality of injection holes (four injection holes in the present embodiment). And a second portion 51 for supplying and distributing the liquid to the first portion 50.
  • the cross section of the flow path that forms the first portion 50 is, for example, circular.
  • the flow path that forms the first part 50 includes a first region 500 that communicates with the injection hole, and a second region 501 that communicates with the first region 500 and communicates with the second region 51.
  • the channel cross-sectional area of the first region 500 is smaller than the channel cross-sectional area of the second region 501. Therefore, the liquid ejected from the first portion 50 is ejected vigorously on the inner peripheral surface 3 by passing through the first region 500.
  • region 500 is equal, and the channel cross-sectional area of each 2nd area
  • the second portion 51 is connected to the first region 510 formed in the cylindrical portion constituting the main body 4 (in the present embodiment, the dissolving portion 40), and the main body 4 (in the present embodiment). Then, the 2nd area
  • the first region 510 is continuous in the circumferential direction of the flow path 2.
  • the first region 510 of the present embodiment has an annular shape when viewed from the central axis direction of the flow path 2.
  • the liquid flowing through the second region 511 is supplied to the first part 50 after passing through the first region 510. Thereby, the liquid flows in the first region 510 in the circumferential direction from the portion of the first region 510 where the second region 511 is connected.
  • the injection unit 5 injects the liquid supplied from the circulation system 10 in a direction having a velocity component from the one end 20 to the other end 21 in the flow path 2.
  • the direction in which the liquid is ejected from the ejection holes of the ejection unit 5 is set so that the liquid ejected from the ejection holes flows smoothly downward in FIGS. 2 and 3. Specifically, the liquid is prevented from being ejected to a portion of the inner peripheral surface 3 where the inclination angle with the central axis ⁇ of the flow path 2 is large, and the intersecting liquid rebounds upward in FIGS. 2 and 3. In order to prevent this, the ejection direction of the liquid from the ejection hole of the ejection unit 5 is set.
  • the liquid ejection direction from the ejection hole of the ejection section 5 intersects at one point on the central axis ⁇ of the flow path 2. Further, in the present embodiment, the location where the injection directions by the injection unit 5 intersect is located at the boundary between the first section 22 and the second section 23 of the flow path 2.
  • the angle between the liquid injection direction ⁇ by the injection unit 5 and the central axis ⁇ of the flow path 2 is the same for all four injection holes.
  • the angle between the liquid ejection direction ⁇ by the ejection unit 5 and the central axis ⁇ of the flow path 2 is 45 ° or less, for example, 40 °.
  • the angle between the liquid ejection direction ⁇ by the ejection unit 5 and the central axis ⁇ of the flow path 2 is such that the first region 231 of the second section 23 in the flow path 2 and the flow path 2 Is larger than the angle between the center axis ⁇ of the two.
  • the ejection unit 5 of the present embodiment ejects liquid into the first section 22 of the flow path 2, that is, the section where the flow path cross-sectional area of the flow path 2 is small.
  • the channel cross-sectional area of the first section 22 of the channel 2 is set to such an extent that the powdery processing agent can be sufficiently dispersed or dissolved in the liquid used for dyeing.
  • the liquid supply unit 7 is formed integrally with the main body 4 (in this embodiment, the connection unit 41).
  • the liquid supply unit 7 of the present embodiment is disposed at a position (a position that is eccentric with respect to the central axis ⁇ of the flow path 2) that is shifted from the center of the cross section in the flow path 2 (the central axis ⁇ of the flow path 2). .
  • the liquid supply unit 7 of the present embodiment supplies liquid along the inner peripheral surface 3 in the circumferential direction of the inner peripheral surface 3 (in the present embodiment, the tangential direction with respect to the inner peripheral surface 3).
  • the liquid is supplied from the circulation system 10 to the liquid supply unit 7 of the present embodiment via the transfer pipe 107 (see FIG. 1).
  • the liquid supply is performed for an arbitrary period.
  • the liquid supply is also performed during a period when the fabric is not treated, for example, during a pot wash.
  • the dispersion unit 8 disperses the treatment agent remaining undissolved in the liquid pushed out from the other end 21 of the flow path 2.
  • the dispersion part 8 includes a cylindrical fixing part 80, a first dispersion member 81, and a second dispersion member 82.
  • the first and second dispersion members 81 each disperse the treatment agent remaining undissolved in the liquid.
  • the other end 401 side of the main body 4 is arranged inside the fixed portion 80.
  • the first dispersion member 81 is provided at the other end 21 of the flow path 2.
  • the first dispersion member 81 of the present embodiment has a disk shape having a plurality of openings 810.
  • the second dispersion member 82 is provided so as to overlap the first dispersion member 81 in the flow direction of the flow path 2 (the vertical direction in FIG. 3, the downward direction in the present embodiment).
  • the second dispersion member 82 of the present embodiment has a disk shape having a plurality of openings 820.
  • the plurality of openings 820 in the second dispersion member 82 and the plurality of openings 810 in the first dispersion member 81 do not overlap (the central axis of the opening 810 and the central axis of the opening 820 are It is arranged so as to shift.
  • the liquid can be circulated through the dispersion portion 8.
  • the liquid can be circulated through the dispersion portion 8 by making a space between the first and second dispersion members 81 and 82.
  • the first dispersion member 81 and the second dispersion member 82 of the present embodiment are disposed in a region surrounded by the fixed portion 80 and the main body 4. Specifically, the first dispersion member 81 and the second dispersion member 82 are supported while being sandwiched between the fixing portion 80 and the main body 4. In the present embodiment, when the liquid is circulated through the dispersion part 8 through the opening 810 of the first dispersion member 81, a turbulent flow is generated in the dispersion part 8. Further, in the present embodiment, the first dispersion member 81 and the second dispersion member 82 are arranged so that the opening 810 of the first dispersion member 81 and the opening 820 of the second dispersion member 82 do not overlap.
  • the liquid moves as follows. First, a powdery processing agent is supplied from the one end 20 of the flow path 2 of the dissolution apparatus 1 by the supply member 11. In the dissolving apparatus 1, a negative pressure is generated due to the ejector effect caused by the liquid ejected from the ejecting unit 5, and thus this treatment agent is sucked into the other end 21 side of the flow path 2 and mixed with the liquid. The liquid in which the treatment agent is mixed is pushed out to the other end 21 of the flow path 2 and moves to the dispersion unit 8.
  • the treatment agent remaining in the liquid is dispersed or dissolved in the liquid by contact with portions other than the openings of the first dispersion member 81 and the second dispersion member 82 and turbulent flow generated in the dispersion unit 8.
  • the liquid that has passed through the dispersing unit 8 is supplied to the main body 1011 of the staying tank 101 via the transfer pipe 108 (see FIG. 1), and is then sucked into the circulation pump 103 from the outlet 1013 of the staying tank 101. Circulate through the circulation system 10.
  • the liquid in the space (flow channel 2) surrounded by the inner peripheral surface 3, the liquid is vigorously ejected to generate a negative pressure due to the ejector effect, and the powder supplied to the space
  • the treatment agent is sucked into the other end 21 of the flow channel 2 and is sufficiently dispersed or dissolved in the liquid.
  • the liquid to be ejected since the liquid to be ejected has a velocity component from the one end 20 to the other end 21 of the flow path 2, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 21. Therefore, the supplied powdery processing agent arrives one after another at a position (in this embodiment, the first section 22) toward which the jetted liquid is directed, and dispersion or dissolution is sequentially performed at this position.
  • the treatment agent is efficiently dispersed or dissolved.
  • the powdery treatment agent is sucked into the other end 21 of the flow path 2.
  • the liquid is more easily brought into contact with the processing agent than when it is ejected toward the second section 23 having a large flow path cross-sectional area.
  • a processing agent and this liquid become easier to mix, and a processing agent can be further disperse
  • the jetted liquid intersects in the first section 22, and thus a negative pressure due to the ejector effect is likely to be generated above the intersecting portion.
  • a processing agent falls efficiently from the supply member 11, a processing agent can be efficiently disperse
  • the cross-sectional area of the first section 22 located between the one end 20 side and the other end 21 side is such that the second section 23 located on the one end 20 side from the first section 22 and the first section It is smaller than the cross-sectional area of the third section 24 located on the other end 21 side from the section 22. Therefore, the processing agent supplied from the one end 20 is easily sucked into the other end 21 side. As a result, the treatment agent and the liquid are easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
  • the liquid supply unit 7 causes the liquid to flow along the inner peripheral surface 3.
  • the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented, it is possible to realize the dissolving device 1 which is not easily contaminated.
  • blockage of the flow path 2 due to the progress of the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented.
  • the liquid supply unit 7 supplies liquid in the circumferential direction of the inner peripheral surface 3. Therefore, since this liquid moves along the circumferential direction of the inner peripheral surface 3 and falls due to gravity, the liquid flows spirally from one end 20 toward the other end 21 as a whole. Thereby, since the adhesion of the treatment agent to a wide range in the circumferential direction of the inner peripheral surface 3 can be prevented, the dissolution apparatus 1 which is not easily contaminated can be realized. Moreover, blockage of the flow path 2 due to the progress of the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented.
  • the injection unit 5 since the injection unit 5 does not protrude into the flow path 2, it is possible to suppress the injection unit 5 from blocking the flow of the powdery processing agent.
  • the ejection unit 5 ejects liquid into the flow path 2 from a plurality of (four in this embodiment) positions spaced in the circumferential direction on the inner circumferential surface 3.
  • the treatment agent even if the treatment agent remains undissolved, it contacts with the first dispersion member 81 and is crushed by this impact, or the treatment agent moves in the moving direction and is dispersed in the liquid in the flow path 2. Or dissolve. Therefore, the treatment agent and the liquid are easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
  • the dissolving apparatus 1 even if the treatment agent remains undissolved, it is further crushed by this impact by contacting the second dispersion member 82, or the movement direction of the treatment agent is changed and the inside of the flow path 2 is changed. To disperse or dissolve in a liquid. Therefore, the treatment agent and the liquid are more easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
  • the processing apparatus 100 including the dissolution apparatus 1 having such a configuration includes the dissolution apparatus 1, a supply member 11 that supplies a powdery treatment agent toward one end 20 of the flow path 2, and a treatment agent from the other end 21 of the flow path 2. And a circulation system 10 to which a liquid in which the liquid is dispersed or dissolved is supplied. Therefore, in the space (flow path 2) surrounded by the inner peripheral surface 3, the liquid processing agent supplied to the space is vigorously ejected, so that the powder processing agent Is sufficiently dispersed or dissolved in this liquid. Moreover, since the liquid to be ejected has a velocity component from one end 20 to the other end 21 of the flow path 2, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 21. As described above, the treatment agent is efficiently dispersed or dissolved.
  • the four injection positions in the injection unit 5 are provided at equal intervals in the circumferential direction, and each of the four injection holes is the same distance as the other end 21 of the flow path 2 in the direction of the central axis ⁇ of the flow path 2. Only provided apart. Further, the angle between the liquid ejection direction ⁇ by the ejection unit 5 and the central axis ⁇ of the flow path 2 is the same for all four ejection positions. As a result, the momentum and amount of the liquid sprayed onto the powdery processing agent are equal to each other, so that the processing agent can be dispersed or dissolved without unevenness.
  • the dissolution apparatus 1001 includes a main body 1004 having an inner peripheral surface 1003 that defines a flow path 1002, an injection unit 1005, a liquid supply unit 7, and a dispersion unit 8.
  • the main body 1004 includes a dispersion or dissolution part 1040 in which the treatment agent is dispersed or dissolved in the liquid, and a connection part 1041 that connects the supply member 11 and the dispersion or dissolution part 1040.
  • the flow path 1002 includes a first section 1024, a second section 1025 located on the one end 1020 side of the first section 1024, and a third section 1026 located on the other end 1023 side of the first section 1024.
  • the channel cross-sectional area of the first section 1024 is the smallest.
  • the ejection unit 1005 of the present embodiment ejects liquid from one position (one through hole) passing through the central axis ⁇ of the flow channel 1002 in a direction from one end 1020 to the other end 1023 in the flow channel 1002. That is, the liquid ejection direction by the ejection unit 1005 of the present embodiment is the same as the flow direction of the powdery processing agent.
  • the through hole of the present embodiment is located near the central axis ⁇ of the flow path 1002.
  • the injection unit 1005 of this embodiment includes a first part 1050 that communicates with one injection hole and has a circular cross section, a second part 1051 that communicates with the first part 1050 and has a circular cross section, and a second part.
  • the first part 1050 and the second part 1051 of this embodiment are provided in the flow path 1002.
  • the third portion 1052 has a cylindrical shape.
  • the third portion 1052 includes a first region 1520 and a second region 1521 that is connected to the first region 1520 and protrudes to the outside of the cylindrical portion that constitutes the main body 1004.
  • the first region 1520 is formed integrally with the main body 1004 (in the present embodiment, the connecting portion 1041).
  • the first region 1520 is connected to the second cylindrical portion 1053 that surrounds the second portion 1051.
  • a first tube portion 1054 surrounding the first portion 1050 is connected to the second tube portion 1053.
  • the liquid flowing through the second region 1521 passes through the first region 1520 and then passes through the first portion 1050 and is injected into the flow path 1002.
  • the inner diameter of the first tube portion 1054 and the flow path cross-sectional area of the first section 1024 in the flow path 1002 are set so that the ejector effect functions effectively.
  • the liquid is vigorously injected into the powdery processing agent supplied to the space in the space (flow path 1002) surrounded by the inner peripheral surface 1003.
  • the powdery treatment agent is sufficiently dispersed or dissolved in this liquid.
  • the liquid to be ejected has a velocity component from one end 1020 to the other end 1023 of the flow path 1002, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 1023. Therefore, the supplied powdery processing agent successively reaches the position where the liquid is ejected, and the processing agent is efficiently dispersed or dissolved by sequentially performing dispersion or dissolution at this position.
  • the surface 1055 located in the direction opposite to the flow direction of the flow path 1002 in the second cylinder portion 1053 (the upward direction in FIG. 4) is convex in this direction and has a smooth shape. Therefore, even if the powdery processing agent supplied from the one end 1020 is placed on the surface 1055 of the second cylindrical portion 1053, it is easily slipped off. Thereby, it can suppress that the injection part 1005 obstruct
  • the melting apparatus 1 according to the present invention is not limited to the configuration of the above embodiment, and various modifications can be made without departing from the gist of the present invention.
  • the flow path cross-sectional area of the third section 24 located closer to the other end 21 than the first section 22 is larger than the flow path cross-sectional area of the first section 22.
  • the channel cross-sectional area of the three sections 24 may be smaller than the channel cross-sectional area of the first section 22 or may be equal to the channel cross-sectional area of the first section 22.
  • the flow path cross-sectional area of the second section 23 located on the one end 20 side of the first section 22 is larger than the flow path cross-sectional area of the first section 22, and the ejection unit 5 flows the liquid. If it injects to the 1st area 22 with a small channel cross-sectional area, it will be easy to contact a processing agent rather than the case where the liquid is injected to the 2nd area 23 with a large channel cross-sectional area. Thereby, a processing agent and this liquid become easier to mix, and a processing agent can be more fully disperse
  • the cross-sectional area of the flow path 2 is uniform at each position in the direction of the central axis ⁇ of the flow path 2, that is, even if the flow path 2 is a cylindrical flow path, it is surrounded by the inner peripheral surface 3.
  • the liquid processing agent is sufficiently dispersed or dissolved in the liquid by vigorously ejecting the liquid to the powder processing agent supplied to the space. .
  • the flow path 2 has a circular cross section, but may have other shapes such as an ellipse or a polygon.
  • the cross section is elliptical or polygonal
  • the central axis of the flow path is an axis passing through the center of gravity of the cross section.
  • the flow path 2 is linear, but a part of the flow path 2 may be curved or may be entirely curved. Even in this case, even if the flow path 2 is not linear, in the space (flow path 2) surrounded by the inner peripheral surface 3, the powdery treatment agent supplied to the space When the liquid is jetted vigorously, the powdery treatment agent is sufficiently dispersed or dissolved in the liquid.
  • the 1st cylinder part 1054 and the 2nd cylinder part which surround the injection part 1005 corresponding to the shape of the flow path 1002. 1053 may be bent. That is, the cylindrical portion surrounding the injection portion 1005 disposed in the bent portion of the flow path 1002 may be partially or wholly bent, and even in this case, When the liquid is jetted vigorously, the powdery treatment agent is sufficiently dispersed or dissolved in the liquid.
  • the liquid supply part 7 is arranged close to the other end 21 of the flow path 2, thereby reducing the size of the dissolution apparatus. Can be achieved.
  • the present invention is not limited to this, and the main body 4 may have a dissolving portion and a connecting portion formed individually.
  • the liquid supply unit 7 may be disposed at a portion where the inner peripheral surface 3 that defines the flow channel 2 is inclined with respect to the central axis ⁇ of the flow channel 2.
  • the plurality of injection holes are provided at equal intervals in the circumferential direction, but may be provided at different intervals.
  • the channel cross-sectional areas of the first regions 510 are equal and the channel cross-sectional areas of the second regions 520 are equal, the amounts of liquid ejected from the four ejection positions were equal.
  • the amount of liquid ejected from the four ejection positions may be varied by varying the channel cross-sectional area and the channel cross-sectional area of the second region 520.
  • the injection hole is located on the inner peripheral surface 3 in the first embodiment, and the injection hole is located near the central axis ⁇ of the flow path 1002 in the second embodiment. And near the central axis of the flow path.
  • each of the four injection holes is provided at a distance equal to the other end 21 of the flow path 2.
  • this distance may not be uniform.
  • the jetting unit is designed so that the angle between the jetting direction ⁇ of the liquid by the jetting unit and the central axis ⁇ of the flow path 2 is different in the four jetting holes. The crossing position in the injection direction can be made one point.
  • the powdery treatment agent supplied from the one end 20 has moved linearly in the direction from the one end 20 to the other end 21 without moving in the flow path 2 in the horizontal direction.
  • the body-like treatment agent may move in the direction from the one end 20 toward the other end 21 while rotating in the flow path 2 in the circumferential direction (moving so as to spiral).
  • the liquid supply unit 7 is supplied with the liquid from the circulation system 10, but the liquid supply unit 7 may be supplied with a liquid from a location (for example, outside) different from the circulation system 10.
  • the liquid supply unit 7 may be supplied with a liquid that is not mixed with the treatment agent and that can disperse or dissolve the treatment agent, for example, water.
  • a liquid that is not mixed with the treatment agent and that can disperse or dissolve the treatment agent for example, water.
  • liquid supply part 7 was distribute
  • the first dispersion member 81 and the second dispersion member 82 are separate members, but they may be integrally formed. In this case, when the first dispersion member and the second dispersion member are assembled, the melting device can be assembled without aligning the openings provided in the first dispersion member and the second dispersion member. It is.
  • the dispersion unit 8 has the two dispersion members, the first dispersion member 81 and the second dispersion member 82, but may have one dispersion member, or three or more of the plurality of dispersion members.
  • the dispersion member may be included. Even in this case, the treatment agent solidified by moisture in the flow path is crushed in contact with the dispersion member, so that the treatment agent and the liquid are easily mixed, and the treatment agent is further dispersed or dissolved in the liquid. be able to.
  • each of the openings 810 and 820 has a circular shape when viewed from the thickness direction of the first dispersion member 81 and the second dispersion member 82.
  • the present invention is not limited to this, and the openings 810 and 820 have an elliptical shape or a polygonal shape. May be.
  • slits may be provided at positions that do not overlap each other.
  • the dispersion part 8 may have a net-like first dispersion member and second dispersion member in which the mesh portions do not overlap each other in a state where the first dispersion member and the second dispersion member are arranged. Even in such a case, the treatment agent solidified by moisture in the flow path is crushed in contact with the dispersion member, so that the treatment agent and the liquid are easily mixed, and the treatment agent is further dispersed or dispersed in the liquid. Can be dissolved.
  • the dissolution apparatus 1 includes the liquid supply unit 7 and the dispersion unit 8, but may not include some or all of them. Even in this case, in the space (flow path 2) surrounded by the inner peripheral surface 3, the liquid is vigorously injected into the powdery processing agent supplied to the space, so that the powder The body treatment agent is sufficiently dispersed or dissolved in the liquid.
  • main body 4, the liquid supply unit 7, and the dispersion unit 8 of the dissolution apparatus 1 may be formed integrally or at least a part thereof may be formed separately.
  • the dissolving device 1 is connected to the circulation system 10 via the transfer pipes 104 to 108, but the dissolving device 1 may be directly connected to the circulation system 10. In this case, since the transfer pipes 104 to 108 are not necessary, the processing apparatus 100 can be downsized.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Treatment Of Fiber Materials (AREA)

Abstract

A treatment agent-dissolving device for a liquid flow-type fabric-treatment apparatus is provided with: a main body having a flow channel configured so that a treatment agent that is in powder form and is used for treating a fabric is supplied to one end and the other end is connected to a circulation system through which a liquid to be used for dyeing is circulated; and a jetting section for jetting the liquid to be used for dyeing into the flow channel in a direction that has a velocity component oriented from the one end of the flow channel to the other end.

Description

液流式布帛処理装置用の処理剤溶解装置、及び、液流式布帛処理装置Treatment agent dissolving device for liquid flow type fabric processing device, and liquid flow type fabric processing device
 本発明は、布帛を処理する液流式布帛処理装置へ、布帛処理用の処理剤を供給するための液流式布帛処理装置用の処理剤溶解装置、及び、液流式布帛処理装置に関する。 The present invention relates to a treatment agent dissolving device for a fluid flow type fabric treatment device for supplying a treatment agent for fabric treatment to a fluid flow type fabric treatment device for treating the fabric, and a fluid flow type fabric treatment device.
 布帛を処理するための布帛処理装置の一つとして、染色に用いる液体を循環させて布帛を処理する液流式布帛処理装置が知られている。従来から、この液流式布帛処理装置に対して、布帛処理用の処理剤を供給するための液流式布帛処理装置用の処理剤溶解装置が提供されている(特許文献1)。 As one of fabric processing apparatuses for processing fabrics, there is known a liquid flow type fabric processing apparatus that circulates a liquid used for dyeing and processes the fabric. Conventionally, a treatment agent dissolving apparatus for a liquid flow type fabric processing apparatus for supplying a treatment agent for fabric treatment to the liquid flow type fabric treatment apparatus has been provided (Patent Document 1).
 図5及び図6に示すように、処理剤溶解装置9100は、染色に用いる液体が循環する循環系統9130を備えた液流式布帛処理装置9000に接続されるものである。具体的には、処理剤溶解装置9100は、処理剤Wが投入される投入口9110が形成された供給槽9120を備え、該供給槽9120は、循環系統9130に直接接続されている。供給槽9120は、投入口9110から処理剤Wが投入されることで、循環系統9130を循環する染色に用いる液体に対して処理剤Wを供給する。 As shown in FIGS. 5 and 6, the treatment agent dissolving apparatus 9100 is connected to a liquid flow type fabric treatment apparatus 9000 provided with a circulation system 9130 through which a liquid used for dyeing circulates. Specifically, the processing agent dissolving apparatus 9100 includes a supply tank 9120 in which an input port 9110 into which the processing agent W is input is formed, and the supply tank 9120 is directly connected to the circulation system 9130. The supply tank 9120 supplies the processing agent W to the liquid used for dyeing that circulates in the circulation system 9130 when the processing agent W is input from the input port 9110.
特開平7-102466号公報JP-A-7-102466
 ところで、処理剤Wの使用量は、処理の対象となる布帛の量や染色に用いる液量に基づいて決定されるものであり、決定された量よりも少ない量で布帛が処理されると、適正に布帛を処理することができないことがある。そのため、予め計量された処理剤Wをロスすることなく、処理剤Wの略全量が、液流式布帛処理装置9000を循環する染色に用いる液体に分散又は溶解することが望まれる、また、処理剤Wが、液体に確実に分散又は溶解することも望まれる。 By the way, the usage amount of the processing agent W is determined based on the amount of the fabric to be processed and the amount of liquid used for dyeing, and when the fabric is processed in an amount smaller than the determined amount, The fabric may not be properly processed. Therefore, it is desired that substantially the entire amount of the processing agent W is dispersed or dissolved in the liquid used for dyeing circulating in the liquid flow type fabric processing device 9000 without losing the pre-measured processing agent W. It is also desirable that the agent W be reliably dispersed or dissolved in the liquid.
 ところが、処理剤溶解装置9100では、供給槽9120は、循環系統9130を構成する配管9140の上部に直接固定されており、処理剤Wは、配管9140よりも上方に位置した投入口9110から、循環する染色に用いる液体中にそのまま投入されることで、処理剤Wの自重により、染色に用いる液体に混合される。この場合、処理剤溶解装置9100では、処理剤Wを染色に用いる液体に対して十分に分散又は溶解する機構が無いために、処理剤Wが十分に分散又は溶解されず、分散又は溶解されていない処理剤が直接布帛に接触することがある。このことが、処理ムラや布帛の汚れの原因になる可能性が有る。 However, in the processing agent dissolving apparatus 9100, the supply tank 9120 is directly fixed to the upper part of the pipe 9140 constituting the circulation system 9130, and the processing agent W is circulated from the input port 9110 positioned above the pipe 9140. By being put in the liquid used for dyeing as it is, it is mixed with the liquid used for dyeing by the dead weight of the processing agent W. In this case, in the treatment agent dissolving apparatus 9100, since there is no mechanism for sufficiently dispersing or dissolving the treatment agent W with respect to the liquid used for dyeing, the treatment agent W is not sufficiently dispersed or dissolved, but is dispersed or dissolved. In some cases, no treatment agent directly contacts the fabric. This may cause processing unevenness and fabric stains.
 そこで、本発明は、かかる実情に鑑み、染色に用いる液体に処理剤を十分に分散又は溶解させることのできる液流式布帛処理装置用の処理剤溶解装置、及び液流式布帛処理装置を提供することを課題とする。 Therefore, in view of such circumstances, the present invention provides a treatment agent dissolving apparatus for a liquid flow type fabric treatment apparatus and a liquid flow type cloth treatment apparatus capable of sufficiently dispersing or dissolving the treatment agent in a liquid used for dyeing. The task is to do.
 本発明にかかる液流式布帛処理装置用の処理剤溶解装置は、粉体状であり且つ布帛を処理する処理剤が一端から供給されると共に、染色に用いる液体が循環する循環系統に他端が接続されるよう構成された流路を有する本体と、前記染色に用いる液体を前記流路内へ該流路の前記一端から前記他端に向かう速度成分を有する方向に噴射する噴射部と、を備える、ことを特徴とする。 The treatment agent dissolving apparatus for the liquid flow type fabric treatment apparatus according to the present invention is in the form of powder and the treatment agent for treating the fabric is supplied from one end, and the other end is connected to the circulation system through which the liquid used for dyeing circulates. A main body having a flow channel configured to be connected, and an ejection unit that ejects the liquid used for staining into the flow channel in a direction having a velocity component from the one end of the flow channel toward the other end, It is characterized by comprising.
 また、前記流路は、第1区間、及び、該第1区間よりも前記一端側に位置する第2区間を有し、前記第1区間の流路断面積は、前記第2区間の流路断面積よりも小さく、前記噴射部は、前記第1区間に向けて、前記染色に用いる液体を噴射してもよい。 The flow path includes a first section and a second section located on the one end side with respect to the first section, and the cross-sectional area of the first section is equal to the flow path of the second section. It is smaller than a cross-sectional area, and the ejection unit may eject the liquid used for the staining toward the first section.
 さらに、前記流路は、前記第1区間よりも前記他端側に位置する第3区間を有し、前記第3区間の流路断面積は、前記第1区間の流路断面積よりも大きくてもよい。 Furthermore, the flow path has a third section located on the other end side with respect to the first section, and the flow path cross-sectional area of the third section is larger than the flow path cross-sectional area of the first section. May be.
 また、前記本体は、前記流路を区画する内周面を有し、前記染色に用いる液体を、前記内周面に沿って供給する液体供給部を備えてもよい。 The main body may have an inner peripheral surface that defines the flow path, and may include a liquid supply unit that supplies the liquid used for the staining along the inner peripheral surface.
 また、前記液体供給部は、前記内周面の周方向に、前記染色に用いる液体を供給してもよい。 Further, the liquid supply unit may supply the liquid used for the staining in the circumferential direction of the inner peripheral surface.
 また、前記本体は、前記流路を区画する内周面を有し、前記噴射部は、前記内周面から前記流路内に前記染色に用いる液体を噴射してもよい。 Further, the main body may have an inner peripheral surface that divides the flow path, and the ejection unit may eject the liquid used for the staining from the inner peripheral surface into the flow path.
 さらに、前記噴射部は、前記内周面における周方向に間隔をあけた複数の位置から、前記流路内に前記染色に用いる液体を噴射してもよい。 Furthermore, the ejection unit may eject the liquid used for the staining into the flow path from a plurality of positions spaced in the circumferential direction on the inner peripheral surface.
 また、前記流路の前記他端に設けられ、複数の開口を有する第1分散部材を備えてもよい。 Further, a first dispersion member provided at the other end of the flow path and having a plurality of openings may be provided.
 さらに、前記流路の流通方向に前記第1分散部材と重ねて、複数の開口を有する第2分散部材が設けられ、前記第2分散部材は、該第2分散部材の複数の開口と前記第1分散部材における前記複数の開口とが重ならないように配置されてもよい。 In addition, a second dispersion member having a plurality of openings is provided so as to overlap the first dispersion member in the flow direction of the flow path, and the second dispersion member includes a plurality of openings of the second dispersion member and the first dispersion member. You may arrange | position so that the said some opening in 1 dispersion | distribution member may not overlap.
 本発明にかかる液流式布帛処理装置は、前記処理剤溶解装置と、前記流路の前記一端に向けて、粉体状の処理剤を供給する供給部材と、前記染色に用いる液体を循環させて、布帛を処理すると共に、前記流路の前記他端から前記染色に用いる液体が供給される循環系統と、を備える、ことを特徴とする。 A liquid flow type fabric treatment apparatus according to the present invention circulates the treatment agent dissolving device, a supply member for supplying a powdery treatment agent toward the one end of the flow path, and a liquid used for the dyeing. And a circulation system for treating the fabric and supplying the liquid used for the dyeing from the other end of the flow path.
図1は、本発明の第1実施形態に係る処理剤溶解装置を備えた液流式布帛処理装置を説明するためのフロー図である。FIG. 1 is a flowchart for explaining a liquid flow type fabric treatment apparatus including a treatment agent dissolving apparatus according to a first embodiment of the present invention. 図2は、同実施形態に係る処理剤溶解装置の外観図である。FIG. 2 is an external view of the treatment agent dissolving apparatus according to the embodiment. 図3は、同実施形態に係る処理剤溶解装置の断面図であって、図2のIII-III断面図である。FIG. 3 is a cross-sectional view of the treatment agent dissolving apparatus according to the embodiment, and is a cross-sectional view taken along the line III-III in FIG. 図4は、本発明の第2実施形態に係る処理剤溶解装置の断面図である。FIG. 4 is a cross-sectional view of the treatment agent dissolving apparatus according to the second embodiment of the present invention. 図5は、従来の処理剤溶解装置を備えた液流式布帛処理装置を説明するためのフロー図である。FIG. 5 is a flowchart for explaining a liquid flow type fabric processing apparatus provided with a conventional processing agent dissolving apparatus. 図6は、従来の処理剤溶解装置における処理剤を循環系統に供給する方法を説明するための模式図である。FIG. 6 is a schematic diagram for explaining a method of supplying a treatment agent to a circulation system in a conventional treatment agent dissolving apparatus.
 以下、本発明の第1実施形態にかかる液流式布帛処理装置100(以下、単に「処理装置100」という)、及び、処理装置100における処理剤溶解装置1(以下、単に「溶解装置1」という)について、図1-図3を参照して説明する。 Hereinafter, the liquid flow type fabric processing apparatus 100 according to the first embodiment of the present invention (hereinafter simply referred to as “processing apparatus 100”) and the processing agent dissolving apparatus 1 (hereinafter simply referred to as “dissolving apparatus 1”) in the processing apparatus 100 will be described. Will be described with reference to FIGS.
 処理装置100において、布帛は、染色に用いる液体により処理される。染色に用いる液体は、布帛処理用の処理剤(布帛を処理する処理剤)が混合された状態の液体を含む。また、染色に用いる液体は、処理剤が未混合状態の液体等も含む。 In the processing apparatus 100, the fabric is processed with a liquid used for dyeing. The liquid used for dyeing includes a liquid in a state where a processing agent for processing a fabric (processing agent for processing the fabric) is mixed. Moreover, the liquid used for dyeing | staining contains the liquid etc. in which a processing agent is not mixed.
 布帛処理用の処理剤は、染色用の染料である。この処理剤は、必要に応じて、布帛に対する染色を促す目的で使用される補助剤(例えば、芒硝(硫酸ナトリウム))、防炎加工用の処理剤等を含む。本実施形態の処理剤は、粉体状の処理剤である。 The treating agent for fabric treatment is a dye for dyeing. This treatment agent includes an auxiliary agent (for example, sodium sulfate (sodium sulfate)) used for the purpose of promoting dyeing of the fabric, a treatment agent for flameproofing, and the like, if necessary. The treatment agent of this embodiment is a powdery treatment agent.
 処理装置100は、染色に用いる液体(以下、単に「液体」と言う。)が循環すると共に布帛を処理する循環系統10と、粉体状の処理剤を供給する供給部材11と、供給部材11から処理剤が供給され且つ液体を循環系統10に供給する溶解装置1と、を備える。 The processing apparatus 100 circulates a liquid used for dyeing (hereinafter simply referred to as “liquid”) and circulates a fabric, a supply system 11 for supplying a powdery processing agent, and a supply member 11. And a dissolving device 1 for supplying a liquid to the circulation system 10.
 循環系統10は、布帛を処理する滞留槽101と、滞留槽101と共に液体の循環系統10を構成する移送管102と、液体を滞留槽101及び移送管102の間で循環させる循環ポンプ103と、を備える。 The circulation system 10 includes a retention tank 101 for treating the fabric, a transfer pipe 102 that forms the liquid circulation system 10 together with the retention tank 101, a circulation pump 103 that circulates the liquid between the retention tank 101 and the transfer pipe 102, Is provided.
 滞留槽101は、布帛を処理する領域となる本体部1011と、液体を本体部1011へ導入する入口部1012と、本体部1011から流出する液体を移送管102に送る出口部1013と、を有する。 The staying tank 101 has a main body portion 1011 serving as a region for processing the fabric, an inlet portion 1012 for introducing the liquid into the main body portion 1011, and an outlet portion 1013 for sending the liquid flowing out from the main body portion 1011 to the transfer pipe 102. .
 移送管102は、滞留槽101の出口部1013と循環ポンプ103の吸込部1031とを繋ぐ第1移送管1021と、循環ポンプ103の吐出部1032及び滞留槽101の入口部1012を繋ぐ第2移送管1022と、を有する。液体は、循環ポンプ103によって昇圧される。そのため、本実施形態では、第2移送管1022内の圧力は、第1移送管1021内の圧力よりも高くなっている。液体は、循環ポンプ103の吐出部1032から吐出されて入口部1012を介して滞留槽101に戻った後、布帛を処理しながら滞留槽101の出口部1013及び第1移送管1021を経由して、循環ポンプ103の吸込部1031へと戻る。このように、処理装置100では、液体が循環している。 The transfer pipe 102 is connected to the first transfer pipe 1021 that connects the outlet 1013 of the retention tank 101 and the suction part 1031 of the circulation pump 103, and the second transfer that connects the discharge part 1032 of the circulation pump 103 and the inlet 1012 of the retention tank 101. A tube 1022. The liquid is pressurized by the circulation pump 103. Therefore, in the present embodiment, the pressure in the second transfer pipe 1022 is higher than the pressure in the first transfer pipe 1021. The liquid is discharged from the discharge portion 1032 of the circulation pump 103 and returns to the retention tank 101 via the inlet portion 1012, and then passes through the outlet portion 1013 of the retention tank 101 and the first transfer pipe 1021 while processing the fabric. Return to the suction portion 1031 of the circulation pump 103. Thus, in the processing apparatus 100, the liquid circulates.
 循環ポンプ103は、液体を吸込む吸込部1031と、液体を送り出す吐出部1032と、を有する。循環系統10からは、移送管104,105が分岐されている。移送管104,105は、移送管106で合流する。移送管106、及び、移送管106から分岐した移送管107は、溶解装置1の上流側に接続されており、移送管106,107から溶解装置1に液体が供給される。また、循環系統10からは、移送管108が分岐されている。移送管108は、溶解装置1の下流側に接続されており、溶解装置1から移送管108を介して循環系統10に液体が供給される。 The circulation pump 103 has a suction part 1031 for sucking liquid and a discharge part 1032 for sending liquid. Transfer pipes 104 and 105 are branched from the circulation system 10. The transfer pipes 104 and 105 merge at the transfer pipe 106. The transfer pipe 106 and the transfer pipe 107 branched from the transfer pipe 106 are connected to the upstream side of the dissolving apparatus 1, and the liquid is supplied to the dissolving apparatus 1 from the transfer pipes 106 and 107. Further, a transfer pipe 108 is branched from the circulation system 10. The transfer pipe 108 is connected to the downstream side of the dissolving apparatus 1, and the liquid is supplied from the dissolving apparatus 1 to the circulation system 10 through the transfer pipe 108.
 供給部材11は、一端から供給された処理剤を貯留すると共に、他端から溶解装置1に前記貯留している処理剤を供給する。本実施形態の供給部材11は、いわゆる、ホッパーである。このようなホッパーの他端部は、例えば、他端に近づくほど縮径する円筒状である。  The supply member 11 stores the processing agent supplied from one end and supplies the stored processing agent to the dissolution apparatus 1 from the other end. The supply member 11 of this embodiment is a so-called hopper. The other end portion of such a hopper is, for example, a cylindrical shape whose diameter is reduced toward the other end.
 溶解装置1は、図2及び図3に示すように、流路2を画定する内周面3を有する本体4と、液体を流路2内に噴射する噴射部5とを備える。本実施形態の本体4は、液体に処理剤を分散又は溶解させる溶解部40と、供給部材11と溶解部40とを連結する連結部41とを有する。具体的には、本体4における溶解部40及び連結部41は一体的に形成されている。連結部41の一端410(図2及び図3における上端)には、供給部材11が接続される。 2 and 3, the melting device 1 includes a main body 4 having an inner peripheral surface 3 that defines a flow path 2 and an injection unit 5 that injects liquid into the flow path 2. The main body 4 of the present embodiment includes a dissolving portion 40 that disperses or dissolves the treatment agent in the liquid, and a connecting portion 41 that connects the supply member 11 and the dissolving portion 40. Specifically, the melting part 40 and the connecting part 41 in the main body 4 are integrally formed. The supply member 11 is connected to one end 410 (the upper end in FIGS. 2 and 3) of the connecting portion 41.
 本実施形態の溶解装置1は、液体を内周面3に沿って供給する液体供給部7を備える。さらに、本実施形態の溶解装置1は、流路2に接続され、流路2から押し出される液体に対して溶け残った処理剤を分散させる分散部8を備える。以下、溶解装置1の各構成について詳細に説明する。 The dissolution apparatus 1 of the present embodiment includes a liquid supply unit 7 that supplies a liquid along the inner peripheral surface 3. Furthermore, the dissolution apparatus 1 of the present embodiment includes a dispersion unit 8 that is connected to the flow path 2 and disperses the treatment agent remaining undissolved in the liquid pushed out from the flow path 2. Hereinafter, each component of the melting apparatus 1 will be described in detail.
 流路2は、内周面3に囲まれた空間である。以下では、便宜上、流路2の形状を説明するが、この説明により、以下の形状の流路2を画定する内周面3の形状を説明することになる。 The flow path 2 is a space surrounded by the inner peripheral surface 3. In the following, for convenience, the shape of the flow path 2 will be described, but this description will explain the shape of the inner peripheral surface 3 that defines the flow path 2 having the following shape.
 流路2の一端20(図3における上端)からは、粉体状の処理剤が供給部材11から供給される。さらに、流路2の他端21(図3における下端)は、移送管108を介して滞留槽101の本体部1011に接続されることで、循環系統10に液体を供給している。 The powdery processing agent is supplied from the supply member 11 from one end 20 (the upper end in FIG. 3) of the flow path 2. Furthermore, the other end 21 (the lower end in FIG. 3) of the flow path 2 is connected to the main body portion 1011 of the staying tank 101 via the transfer pipe 108 to supply the liquid to the circulation system 10.
 本実施形態の流路2の断面は、例えば、円状である。なお、ここでいう「流路2の断面」とは、流路2の中心軸αに直交する方向の断面を言う。また、本実施形態の流路2は、溶解部40において、第1区間22、第1区間22よりも一端20側に位置する第2区間23、及び、第1区間22よりも他端21側に位置する第3区間24を有する。溶解部40では、流路2の一端20から他端21に向けて、第2区間23と、第1区間22と、第3区間24とが順に位置している。 The cross section of the flow path 2 of the present embodiment is, for example, circular. Here, the “cross section of the flow path 2” refers to a cross section in a direction perpendicular to the central axis α of the flow path 2. In addition, the flow path 2 of the present embodiment includes the first section 22, the second section 23 located on the one end 20 side of the first section 22, and the other end 21 side of the first section 22 in the dissolving section 40. A third section 24 located at In the melting part 40, the second section 23, the first section 22, and the third section 24 are positioned in order from the one end 20 to the other end 21 of the flow path 2.
 第1区間22の流路断面積は、第2区間23の流路断面積よりも小さい。第3区間24の流路断面積は、第1区間22の流路断面積よりも大きい。即ち、一端20側と他端21側との間に位置する第1区間22の流路断面積が、一端20側に位置する第2区間23及び他端21側に位置する第3区間24の流路断面積より小さい。 The flow path cross-sectional area of the first section 22 is smaller than that of the second section 23. The cross-sectional area of the third section 24 is larger than the cross-sectional area of the first section 22. That is, the cross-sectional area of the first section 22 located between the one end 20 side and the other end 21 side is the second section 23 located on the one end 20 side and the third section 24 located on the other end 21 side. It is smaller than the cross-sectional area of the channel.
 第2区間23は、一端20側に位置する第1領域231と、一端20側及び他端21側の間に位置する第2領域232と、他端21側に位置する第3領域233とを有する。流路2の一端20から他端21に向けて、第1領域231と、第2領域232と、第3領域233とが順に接続されている。第1領域231の流路断面積は、他端21側に近づくほど小さくなる。即ち、第1領域231は、他端21側に近づくほど縮径している。本実施形態では、第1領域231の傾斜角(内周面3における第1領域231を区画する部分と、流路2の中心軸αに直交する方向(図3における水平方向)との間の角度θ1)は、粉体状の処理剤の安息角よりも大きい。このように、第1領域231の傾斜角が粉体状の処理剤の安息角よりも大きいため、粉体状の処理剤は、内周面3における第1領域231を区画する部分を滑り落ちやすい。 The second section 23 includes a first region 231 located on the one end 20 side, a second region 232 located between the one end 20 side and the other end 21 side, and a third region 233 located on the other end 21 side. Have. A first region 231, a second region 232, and a third region 233 are sequentially connected from one end 20 to the other end 21 of the flow path 2. The channel cross-sectional area of the first region 231 decreases as it approaches the other end 21 side. That is, the diameter of the first region 231 decreases toward the other end 21 side. In the present embodiment, the inclination angle of the first region 231 (between the portion defining the first region 231 on the inner peripheral surface 3 and the direction perpendicular to the central axis α of the flow path 2 (horizontal direction in FIG. 3)). The angle θ1) is larger than the angle of repose of the powdery treatment agent. As described above, since the inclination angle of the first region 231 is larger than the angle of repose of the powdery treatment agent, the powdery treatment agent slides down the portion defining the first region 231 on the inner peripheral surface 3. Cheap.
 第2領域232の傾斜角(内周面3における第2領域232を区画する部分と、流路2の中心軸αに直交する方向(図3における水平方向)との間の角度θ2)は、粉体状の処理剤の安息角よりも大きい。そのため、第1領域231と同様の理由により、粉体状の処理剤は、内周面3における第2領域232を区画する部分を滑り落ちやすい。なお、θ2は、粉体状の処理剤の安息角よりも大きく、90°以下であることが好ましい。さらに、第2領域232には、流路2内に液体を噴射する噴射孔が設けられている。 The inclination angle of the second region 232 (the angle θ2 between the portion defining the second region 232 on the inner peripheral surface 3 and the direction orthogonal to the central axis α of the flow channel 2 (horizontal direction in FIG. 3)) It is larger than the angle of repose of the powdery treatment agent. Therefore, for the same reason as in the first region 231, the powdery treatment agent easily slides down the portion defining the second region 232 on the inner peripheral surface 3. In addition, it is preferable that (theta) 2 is larger than the angle of repose of a powdery processing agent, and is 90 degrees or less. Further, the second region 232 is provided with an injection hole for injecting liquid into the flow path 2.
 第3領域233の流路断面積は、他端21に近づくほど小さくなる。即ち、第3領域233は、他端21側に近づくほど縮径している。本実施形態では、第3領域233の傾斜角(内周面3における第3領域233を区画する部分と、流路2の中心軸αに直交する方向(図3における水平方向)との間の角度θ3)は、粉体状の処理剤の安息角よりも大きい。そのため、第1領域231と同様の理由により、粉体状の処理剤は、内周面3における第3領域233を区画する部分を滑り落ちやすい。 The flow path cross-sectional area of the third region 233 decreases as it approaches the other end 21. That is, the diameter of the third region 233 decreases as it approaches the other end 21 side. In the present embodiment, the inclination angle of the third region 233 (between the portion defining the third region 233 on the inner peripheral surface 3 and the direction perpendicular to the central axis α of the flow path 2 (horizontal direction in FIG. 3)). The angle θ3) is larger than the angle of repose of the powdery treatment agent. Therefore, for the same reason as in the first region 231, the powdery treatment agent easily slides down the portion that partitions the third region 233 on the inner peripheral surface 3.
 流路2において、第2区間22の流路断面積は、最も小さくなっている。 In the flow path 2, the cross-sectional area of the second section 22 is the smallest.
 第3区間24は、一端20側に位置する第1領域241と、他端21側に位置する第2領域242を有する。 The third section 24 has a first region 241 located on the one end 20 side and a second region 242 located on the other end 21 side.
 第1領域241の流路断面積は、他端21側に近づくほど大きくなる。即ち、第1領域241は、他端21側に近づくほど拡径している。 The flow path cross-sectional area of the first region 241 increases as it approaches the other end 21 side. That is, the diameter of the first region 241 increases as it approaches the other end 21 side.
 同様に、第2領域242の流路断面積は、他端21側に近づくほど大きくなる。即ち、第2領域242は、他端21側に近づくほど拡径している。また、第2領域242の傾斜角(内周面3における第2領域242を区画する部分と、流路2の中心軸αに直交する方向(図3における水平方向)との間の角度θ5)は、第1領域241の傾斜角(内周面3における第1領域241を区画する部分と、流路2の中心軸αに直交する方向(図3における水平方向)との間の角度θ4)よりも大きい。 Similarly, the flow path cross-sectional area of the second region 242 increases as it approaches the other end 21 side. That is, the diameter of the second region 242 increases as it approaches the other end 21 side. Further, the inclination angle of the second region 242 (the angle θ5 between the portion defining the second region 242 on the inner peripheral surface 3 and the direction perpendicular to the central axis α of the flow path 2 (horizontal direction in FIG. 3)) Is the inclination angle of the first region 241 (the angle θ4 between the portion defining the first region 241 on the inner peripheral surface 3 and the direction perpendicular to the central axis α of the flow path 2 (horizontal direction in FIG. 3)) Bigger than.
 本実施形態の流路2が以上の構成であるため、一端20から供給された粉体状の処理剤は、流路2内において、水平方向(図3における水平方向)には移動せず、一端20から他端21に向かう方向に直線的に移動する。 Since the flow path 2 of the present embodiment has the above-described configuration, the powdery processing agent supplied from the one end 20 does not move in the horizontal direction (the horizontal direction in FIG. 3) in the flow path 2, It moves linearly in the direction from the one end 20 toward the other end 21.
 噴射部5は、循環系統10のうち他端21が接続される部分よりも上流部分に接続される。本実施形態の噴射部5には、移送管106(図1参照)を介して、循環系統10から液体が供給されている。 The injection unit 5 is connected to the upstream part of the circulation system 10 than the part to which the other end 21 is connected. Liquid is supplied from the circulation system 10 to the injection unit 5 of the present embodiment via the transfer pipe 106 (see FIG. 1).
 本実施形態の噴射部5は、上述のように、内周面3から流路2内に液体を噴射する。本実施形態では、噴射部5は、内周面3における周方向に間隔をあけた複数の位置(本実施形態では、四つの噴射孔)から、流路2内に液体を噴射する。本実施形態では、四つの噴射孔は、周方向に等間隔をあけて設けられている。また、本実施形態では、流路2の中心軸α方向において、四つの噴射孔のそれぞれは、流路2の他端21と等しい距離だけ離れて設けられている。 The injection unit 5 of the present embodiment injects liquid from the inner peripheral surface 3 into the flow path 2 as described above. In the present embodiment, the ejection unit 5 ejects the liquid into the flow path 2 from a plurality of positions (four injection holes in the present embodiment) spaced in the circumferential direction on the inner peripheral surface 3. In the present embodiment, the four injection holes are provided at equal intervals in the circumferential direction. In the present embodiment, in the direction of the central axis α of the flow path 2, each of the four injection holes is provided at a distance equal to the other end 21 of the flow path 2.
 本実施形態の噴射部5は、複数の噴射孔(本実施形態では、四つの噴射孔)とそれぞれ連通する複数の流路(本実施形態では、四つの流路)からなる第1部位50と、第1部位50に液体を供給すると共に分配する第2部位51とを有する。 The injection unit 5 of the present embodiment includes a first portion 50 composed of a plurality of flow paths (four flow paths in the present embodiment) respectively communicating with a plurality of injection holes (four injection holes in the present embodiment). And a second portion 51 for supplying and distributing the liquid to the first portion 50.
 第1部位50は、本体4(本実施形態では、溶解部40)を構成する筒部分の内部に形成されている。第1部位50を構成する流路の断面は、例えば、円状である。第1部位50を構成する流路は、噴射孔から連通する第1領域500と、第1領域500に連通し、且つ、第2部位51に連通する第2領域501とを有する。第1領域500の流路断面積は、第2領域501の流路断面積よりも小さい。そのため、第1部位50から噴射される液体は、第1領域500を通ることで、内周面3に勢いよく噴射される。なお、第1領域500それぞれの流路断面積が等しく、且つ、第2領域501それぞれの流路断面積が等しいため、四つの噴射孔から噴射される液体の量は等しい。 1st site | part 50 is formed in the inside of the cylinder part which comprises the main body 4 (this embodiment melt | dissolution part 40). The cross section of the flow path that forms the first portion 50 is, for example, circular. The flow path that forms the first part 50 includes a first region 500 that communicates with the injection hole, and a second region 501 that communicates with the first region 500 and communicates with the second region 51. The channel cross-sectional area of the first region 500 is smaller than the channel cross-sectional area of the second region 501. Therefore, the liquid ejected from the first portion 50 is ejected vigorously on the inner peripheral surface 3 by passing through the first region 500. In addition, since the channel cross-sectional area of each 1st area | region 500 is equal, and the channel cross-sectional area of each 2nd area | region 501 is equal, the quantity of the liquid injected from four injection holes is equal.
 第2部位51は、本体4(本実施形態では、溶解部40)を構成する筒部分の内部に形成されている第1領域510と、第1領域510に接続され且つ本体4(本実施形態では、溶解部40)を構成する筒部分の外部に突出した第2領域511とを含む。第1領域510は、流路2の周方向に連続している。本実施形態の第1領域510は、流路2の中心軸方向から視ると円環状である。 The second portion 51 is connected to the first region 510 formed in the cylindrical portion constituting the main body 4 (in the present embodiment, the dissolving portion 40), and the main body 4 (in the present embodiment). Then, the 2nd area | region 511 which protruded outside the cylinder part which comprises the melt | dissolution part 40) is included. The first region 510 is continuous in the circumferential direction of the flow path 2. The first region 510 of the present embodiment has an annular shape when viewed from the central axis direction of the flow path 2.
 第2領域511を流通する液体は、第1領域510を通った後、第1部位50に供給される。これにより、液体が、第1領域510における第2領域511が接続されている部分から、第1領域510内を周方向に流通する。 The liquid flowing through the second region 511 is supplied to the first part 50 after passing through the first region 510. Thereby, the liquid flows in the first region 510 in the circumferential direction from the portion of the first region 510 where the second region 511 is connected.
 噴射部5は、循環系統10から供給された液体を、流路2内の一端20から他端21に向かう速度成分を有する方向に噴射する。噴射部5の噴射孔からの液体の噴射方向は、噴射孔から噴射された液体がスムースに図2及び図3における下方向に流れるよう設定されている。具体的には、液体が内周面3のうち流路2の中心軸αとの傾斜角が大きい箇所に噴射されることを防止し、交差した液体が図2及び図3における上方向に跳ね返ることを防止できるよう、噴射部5の噴射孔からの液体の噴射方向が設定されている。本実施形態では、噴射部5の噴射孔からの液体の噴射方向は、流路2の中心軸α上の一点で交差する。また、本実施形態では、噴射部5による噴射方向が交差する箇所は、流路2の第1区間22と第2区間23との境界に位置する。 The injection unit 5 injects the liquid supplied from the circulation system 10 in a direction having a velocity component from the one end 20 to the other end 21 in the flow path 2. The direction in which the liquid is ejected from the ejection holes of the ejection unit 5 is set so that the liquid ejected from the ejection holes flows smoothly downward in FIGS. 2 and 3. Specifically, the liquid is prevented from being ejected to a portion of the inner peripheral surface 3 where the inclination angle with the central axis α of the flow path 2 is large, and the intersecting liquid rebounds upward in FIGS. 2 and 3. In order to prevent this, the ejection direction of the liquid from the ejection hole of the ejection unit 5 is set. In the present embodiment, the liquid ejection direction from the ejection hole of the ejection section 5 intersects at one point on the central axis α of the flow path 2. Further, in the present embodiment, the location where the injection directions by the injection unit 5 intersect is located at the boundary between the first section 22 and the second section 23 of the flow path 2.
 本実施形態では、噴射部5による液体の噴射方向βと、流路2の中心軸αとの間の角度は、四つの噴射孔いずれについても等しい。また、本実施形態では、噴射部5による液体の噴射方向βと、流路2の中心軸αとの間の角度は、45°以下であり、例えば、40°である。さらに、本実施形態では、噴射部5による液体の噴射方向βと、流路2の中心軸αとの間の角度は、流路2における第2区間23の第1領域231と、流路2の中心軸αとの間の角度よりも大きい。 In the present embodiment, the angle between the liquid injection direction β by the injection unit 5 and the central axis α of the flow path 2 is the same for all four injection holes. In the present embodiment, the angle between the liquid ejection direction β by the ejection unit 5 and the central axis α of the flow path 2 is 45 ° or less, for example, 40 °. Furthermore, in the present embodiment, the angle between the liquid ejection direction β by the ejection unit 5 and the central axis α of the flow path 2 is such that the first region 231 of the second section 23 in the flow path 2 and the flow path 2 Is larger than the angle between the center axis α of the two.
 本実施形態の噴射部5は、流路2の第1区間22、即ち、流路2の流路断面積が小さい区間に液体を噴射する。なお、流路2の第1区間22の流路断面積は、粉体状の処理剤が染色に用いる液体に対して、十分に分散又は溶解できる程度に設定されている。 The ejection unit 5 of the present embodiment ejects liquid into the first section 22 of the flow path 2, that is, the section where the flow path cross-sectional area of the flow path 2 is small. The channel cross-sectional area of the first section 22 of the channel 2 is set to such an extent that the powdery processing agent can be sufficiently dispersed or dissolved in the liquid used for dyeing.
 液体供給部7は、図3に示すように、本体4(本実施形態では、連結部41)と一体的に形成されている。本実施形態の液体供給部7は、流路2内における断面の中心(流路2の中心軸α)からずれた位置(流路2の中心軸αに対して偏心した位置)に配される。具体的には、本実施形態の液体供給部7は、内周面3に沿って内周面3の周方向(本実施形態では、内周面3に対する接線方向)に、液体を供給する。また、本実施形態の液体供給部7には、移送管107(図1参照)を介して、循環系統10から液体が供給されている。液体の供給は、任意の期間に実施される。また、液体の供給は、布帛の処置を行わない期間、例えば、釜洗い等の期間にも実施される。 As shown in FIG. 3, the liquid supply unit 7 is formed integrally with the main body 4 (in this embodiment, the connection unit 41). The liquid supply unit 7 of the present embodiment is disposed at a position (a position that is eccentric with respect to the central axis α of the flow path 2) that is shifted from the center of the cross section in the flow path 2 (the central axis α of the flow path 2). . Specifically, the liquid supply unit 7 of the present embodiment supplies liquid along the inner peripheral surface 3 in the circumferential direction of the inner peripheral surface 3 (in the present embodiment, the tangential direction with respect to the inner peripheral surface 3). In addition, the liquid is supplied from the circulation system 10 to the liquid supply unit 7 of the present embodiment via the transfer pipe 107 (see FIG. 1). The liquid supply is performed for an arbitrary period. The liquid supply is also performed during a period when the fabric is not treated, for example, during a pot wash.
 分散部8は、流路2の他端21から押し出される液体に溶け残った処理剤を分散させる。本実施形態では、分散部8は、円筒状の固定部80と、第1分散部材81と、第2分散部材82とを有する。第1、第2分散部材81は、それぞれ、液体に溶け残った処理剤を分散させる。 The dispersion unit 8 disperses the treatment agent remaining undissolved in the liquid pushed out from the other end 21 of the flow path 2. In the present embodiment, the dispersion part 8 includes a cylindrical fixing part 80, a first dispersion member 81, and a second dispersion member 82. The first and second dispersion members 81 each disperse the treatment agent remaining undissolved in the liquid.
 本実施形態では、固定部80の内側に、本体4の他端401側に配されている。第1分散部材81は、流路2の他端21に設けられている。本実施形態の第1分散部材81は、複数の開口810を有する円板状である。第2分散部材82は、流路2の流通方向(図3における縦方向、本実施形態では、下方向)に第1分散部材81と重ねて設けられている。本実施形態の第2分散部材82は、複数の開口820を有する円板状である。また、本発明の第2分散部材82は、第2分散部材82における複数の開口820と第1分散部材81における複数の開口810とが重ならない(開口810の中心軸と開口820の中心軸がずれる)ように配置されている。 In the present embodiment, the other end 401 side of the main body 4 is arranged inside the fixed portion 80. The first dispersion member 81 is provided at the other end 21 of the flow path 2. The first dispersion member 81 of the present embodiment has a disk shape having a plurality of openings 810. The second dispersion member 82 is provided so as to overlap the first dispersion member 81 in the flow direction of the flow path 2 (the vertical direction in FIG. 3, the downward direction in the present embodiment). The second dispersion member 82 of the present embodiment has a disk shape having a plurality of openings 820. In the second dispersion member 82 of the present invention, the plurality of openings 820 in the second dispersion member 82 and the plurality of openings 810 in the first dispersion member 81 do not overlap (the central axis of the opening 810 and the central axis of the opening 820 are It is arranged so as to shift.
 本実施形態では、第1、第2分散部材81,82の間に空間が存在しているが、開口810の一部が開口820と重なっていれば、第1、第2分散部材81,82の間に空間が存在していなくても(即ち、第1、第2分散部材81,82が密着していても)、分散部8に液体を流通させることができる。なお、開口810の全部が開口820の全部と重ならない場合は、第1、第2分散部材81,82の間に空間を存在させることで、分散部8に液体を流通させることができる。 In this embodiment, there is a space between the first and second dispersion members 81 and 82, but if a part of the opening 810 overlaps the opening 820, the first and second dispersion members 81 and 82 are present. Even if there is no space between them (that is, even if the first and second dispersion members 81 and 82 are in close contact with each other), the liquid can be circulated through the dispersion portion 8. In addition, when all of the openings 810 do not overlap with all of the openings 820, the liquid can be circulated through the dispersion portion 8 by making a space between the first and second dispersion members 81 and 82.
 本実施形態の第1分散部材81及び第2分散部材82は、固定部80及び本体4で囲まれた領域に配置されている。具体的には、第1分散部材81及び第2分散部材82は、固定部80及び本体4に挟まれた状態で支持されている。また、本実施形態では、第1分散部材81の開口810により、液体を分散部8に流通させると分散部8で乱流が生じる。さらに、本実施形態では、第1分散部材81の開口810及び第2分散部材82の開口820が重ならないように第1分散部材81及び第2分散部材82が配置されている。 The first dispersion member 81 and the second dispersion member 82 of the present embodiment are disposed in a region surrounded by the fixed portion 80 and the main body 4. Specifically, the first dispersion member 81 and the second dispersion member 82 are supported while being sandwiched between the fixing portion 80 and the main body 4. In the present embodiment, when the liquid is circulated through the dispersion part 8 through the opening 810 of the first dispersion member 81, a turbulent flow is generated in the dispersion part 8. Further, in the present embodiment, the first dispersion member 81 and the second dispersion member 82 are arranged so that the opening 810 of the first dispersion member 81 and the opening 820 of the second dispersion member 82 do not overlap.
 上述した構成により、処理装置100では、液体が以下のように移動する。まず、供給部材11により、粉体状の処理剤が、溶解装置1の流路2の一端20から供給される。溶解装置1では、噴射部5から噴射された液体によるエジェクター効果により負圧が生じるため、この処理剤は、流路2の他端21側に吸い込まれ、液体と混ざる。処理剤が混ざった状態の液体は、流路2の他端21に押し出されて、分散部8に移動する。分散部8において、液体に溶け残った処理剤は、第1分散部材81及び第2分散部材82の開口以外の部分への接触、及び、分散部8で生じる乱流により、液体に分散又は溶解する。分散部8を通過した液体は、移送管108(図1参照)を介して、滞留槽101の本体部1011に供給された後、さらに、滞留槽101の出口部1013から循環ポンプ103に吸い込まれ、循環系統10を循環する。 With the above-described configuration, in the processing apparatus 100, the liquid moves as follows. First, a powdery processing agent is supplied from the one end 20 of the flow path 2 of the dissolution apparatus 1 by the supply member 11. In the dissolving apparatus 1, a negative pressure is generated due to the ejector effect caused by the liquid ejected from the ejecting unit 5, and thus this treatment agent is sucked into the other end 21 side of the flow path 2 and mixed with the liquid. The liquid in which the treatment agent is mixed is pushed out to the other end 21 of the flow path 2 and moves to the dispersion unit 8. In the dispersion unit 8, the treatment agent remaining in the liquid is dispersed or dissolved in the liquid by contact with portions other than the openings of the first dispersion member 81 and the second dispersion member 82 and turbulent flow generated in the dispersion unit 8. To do. The liquid that has passed through the dispersing unit 8 is supplied to the main body 1011 of the staying tank 101 via the transfer pipe 108 (see FIG. 1), and is then sucked into the circulation pump 103 from the outlet 1013 of the staying tank 101. Circulate through the circulation system 10.
 続いて、上記構成の溶解装置1の作用及び効果について説明する。 Subsequently, the operation and effect of the dissolution apparatus 1 having the above configuration will be described.
 かかる構成の溶解装置1では、内周面3に囲まれた空間(流路2)内において、液体が勢いよく噴射されることでエジェクター効果による負圧が生じ、該空間に供給された粉体状の処理剤は、流路2の他端21に吸い込まれて、液体に十分に分散又は溶解する。しかも、噴射される液体が、流路2の一端20から他端21に向かう速度成分を有することで、粉体状の処理剤が分散又は溶解した液体が他端21から押し出される。そのため、噴射された液体が向かう位置(本実施形態では、第1区間22)に、供給された粉体状の処理剤が次々に到達し、この位置で分散又は溶解が順次行われることで、処理剤が効率よく分散又は溶解される。 In the melting device 1 having such a configuration, in the space (flow channel 2) surrounded by the inner peripheral surface 3, the liquid is vigorously ejected to generate a negative pressure due to the ejector effect, and the powder supplied to the space The treatment agent is sucked into the other end 21 of the flow channel 2 and is sufficiently dispersed or dissolved in the liquid. In addition, since the liquid to be ejected has a velocity component from the one end 20 to the other end 21 of the flow path 2, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 21. Therefore, the supplied powdery processing agent arrives one after another at a position (in this embodiment, the first section 22) toward which the jetted liquid is directed, and dispersion or dissolution is sequentially performed at this position. The treatment agent is efficiently dispersed or dissolved.
 溶解装置1では、液体が流路断面積の小さい第1区間22に向けて噴射されることで、エジェクター効果が高まるため、粉体状の処理剤は、流路2の他端21に吸い込まれて液体にさらに分散又は溶解する。しかも、液体が流路断面積の小さい第1区間22に向けて噴射されることで、流路断面積の大きい第2区間23に向けて噴射される場合よりも、処理剤と接触しやすい。これにより、処理剤とこの液体とがより混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 In the dissolving apparatus 1, since the ejector effect is enhanced by ejecting the liquid toward the first section 22 having a small flow path cross-sectional area, the powdery treatment agent is sucked into the other end 21 of the flow path 2. To further disperse or dissolve in the liquid. In addition, since the liquid is ejected toward the first section 22 having a small flow path cross-sectional area, the liquid is more easily brought into contact with the processing agent than when it is ejected toward the second section 23 having a large flow path cross-sectional area. Thereby, a processing agent and this liquid become easier to mix, and a processing agent can be further disperse | distributed or dissolved in a liquid.
 溶解装置1では、噴射された液体が第1区間22で交差することで、この交差する箇所よりも上部でエジェクター効果による負圧が生じやすい。これにより、供給部材11から処理剤が効率よく落下するため、液体に処理剤を効率的に分散又は溶解させることができる。 In the dissolution apparatus 1, the jetted liquid intersects in the first section 22, and thus a negative pressure due to the ejector effect is likely to be generated above the intersecting portion. Thereby, since a processing agent falls efficiently from the supply member 11, a processing agent can be efficiently disperse | distributed or dissolved in a liquid.
 しかも、溶解装置1では、一端20側と他端21側との間に位置する第1区間22の断面積が、第1区間22より一端20側に位置する第2区間23、及び、第1区間22より他端21側に位置する第3区間24の断面積より小さい。そのため、一端20から供給された処理剤が他端21側に吸い込まれやすい。これにより、処理剤と液体とが混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 Moreover, in the melting apparatus 1, the cross-sectional area of the first section 22 located between the one end 20 side and the other end 21 side is such that the second section 23 located on the one end 20 side from the first section 22 and the first section It is smaller than the cross-sectional area of the third section 24 located on the other end 21 side from the section 22. Therefore, the processing agent supplied from the one end 20 is easily sucked into the other end 21 side. As a result, the treatment agent and the liquid are easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
 溶解装置1では、液体供給部7が、液体を内周面3に沿って流す。これにより、処理剤の内周面3への付着を防ぐことができるため、汚れにくい溶解装置1を実現することができる。また、処理剤の内周面3への付着の進行に起因する流路2の閉塞も防ぐことができる。 In the melting apparatus 1, the liquid supply unit 7 causes the liquid to flow along the inner peripheral surface 3. Thereby, since the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented, it is possible to realize the dissolving device 1 which is not easily contaminated. Moreover, blockage of the flow path 2 due to the progress of the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented.
 溶解装置1では、液体供給部7が、内周面3の周方向に液体を供給する。そのため、この液体は、内周面3の周方向に沿って移動すると共に重力により落下するため、全体として螺旋状に移動しつつ一端20から他端21に向かって流れることになる。これにより、内周面3の周方向における広い範囲への処理剤の付着を防ぐことができるため、汚れにくい溶解装置1を実現することができる。また、処理剤の内周面3への付着の進行に起因する流路2の閉塞も防ぐことができる。 In the melting apparatus 1, the liquid supply unit 7 supplies liquid in the circumferential direction of the inner peripheral surface 3. Therefore, since this liquid moves along the circumferential direction of the inner peripheral surface 3 and falls due to gravity, the liquid flows spirally from one end 20 toward the other end 21 as a whole. Thereby, since the adhesion of the treatment agent to a wide range in the circumferential direction of the inner peripheral surface 3 can be prevented, the dissolution apparatus 1 which is not easily contaminated can be realized. Moreover, blockage of the flow path 2 due to the progress of the adhesion of the treatment agent to the inner peripheral surface 3 can be prevented.
 溶解装置1では、噴射部5が流路2内に突出していないため、噴射部5が粉体状の処理剤の流れを遮ることを抑制できる。 In the melting apparatus 1, since the injection unit 5 does not protrude into the flow path 2, it is possible to suppress the injection unit 5 from blocking the flow of the powdery processing agent.
 溶解装置1では、噴射部5が、内周面3における周方向に間隔をあけた複数(本実施形態では四つ)の位置から、流路2内に液体を噴射する。これにより、液体が異なる方向から処理剤に噴射されるため、処理剤と液体とが混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 In the melting apparatus 1, the ejection unit 5 ejects liquid into the flow path 2 from a plurality of (four in this embodiment) positions spaced in the circumferential direction on the inner circumferential surface 3. Thereby, since a liquid is injected to a processing agent from a different direction, it becomes easy to mix a processing agent and a liquid, and a processing agent can be further disperse | distributed or dissolved in a liquid.
 溶解装置1では、処理剤が溶け残っても、第1分散部材81に接触することで、この衝撃により粉砕される、又は、処理剤の移動方向が変化して流路2内で液体に分散又は溶解する。そのため、処理剤と液体とが混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 In the dissolution apparatus 1, even if the treatment agent remains undissolved, it contacts with the first dispersion member 81 and is crushed by this impact, or the treatment agent moves in the moving direction and is dispersed in the liquid in the flow path 2. Or dissolve. Therefore, the treatment agent and the liquid are easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
 さらに、溶解装置1では、処理剤が溶け残っても、さらに、第2分散部材82に接触することで、この衝撃により粉砕される、又は、処理剤の移動方向が変化して流路2内で液体に分散又は溶解する。そのため、処理剤と液体とがさらに混ざりやすく、液体に処理剤をさらに分散又は溶解させることができる。 Further, in the dissolving apparatus 1, even if the treatment agent remains undissolved, it is further crushed by this impact by contacting the second dispersion member 82, or the movement direction of the treatment agent is changed and the inside of the flow path 2 is changed. To disperse or dissolve in a liquid. Therefore, the treatment agent and the liquid are more easily mixed, and the treatment agent can be further dispersed or dissolved in the liquid.
 かかる構成の溶解装置1を備える処理装置100は、溶解装置1と、流路2の一端20に向けて粉状の処理剤を供給する供給部材11と、流路2の他端21から処理剤を分散又は溶解させた液体が供給される循環系統10とを備える。そのため、内周面3に囲まれた空間(流路2)内において、該空間に供給されている粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。しかも、噴射される液体が、流路2の一端20から他端21への速度成分を有することで、粉体状の処理剤が分散又は溶解した液体が他端21から押し出されるため、上述したように、処理剤が効率よく分散又は溶解される。 The processing apparatus 100 including the dissolution apparatus 1 having such a configuration includes the dissolution apparatus 1, a supply member 11 that supplies a powdery treatment agent toward one end 20 of the flow path 2, and a treatment agent from the other end 21 of the flow path 2. And a circulation system 10 to which a liquid in which the liquid is dispersed or dissolved is supplied. Therefore, in the space (flow path 2) surrounded by the inner peripheral surface 3, the liquid processing agent supplied to the space is vigorously ejected, so that the powder processing agent Is sufficiently dispersed or dissolved in this liquid. Moreover, since the liquid to be ejected has a velocity component from one end 20 to the other end 21 of the flow path 2, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 21. As described above, the treatment agent is efficiently dispersed or dissolved.
 噴射部5における四つの噴射位置は、周方向に等間隔をあけて設けられると共に、流路2の中心軸α方向において、四つの噴射孔のそれぞれは、流路2の他端21と等しい距離だけ離れて設けられている。また、噴射部5による液体の噴射方向βと、流路2の中心軸αとの間の角度は、四つの噴射位置いずれについても等しい。これにより、粉体状の処理剤に液体が噴射される勢いや噴射される量がそれぞれ等しくなるため、処理剤を偏りなく分散又は溶解させることができる。 The four injection positions in the injection unit 5 are provided at equal intervals in the circumferential direction, and each of the four injection holes is the same distance as the other end 21 of the flow path 2 in the direction of the central axis α of the flow path 2. Only provided apart. Further, the angle between the liquid ejection direction β by the ejection unit 5 and the central axis α of the flow path 2 is the same for all four ejection positions. As a result, the momentum and amount of the liquid sprayed onto the powdery processing agent are equal to each other, so that the processing agent can be dispersed or dissolved without unevenness.
 以下、第2実施形態にかかる処理剤溶解装置について、図4を用いて説明する。第2実施形態の構成のうち第1実施形態と同じ構成については、同一の符号を付す。 Hereinafter, the processing agent dissolution apparatus according to the second embodiment will be described with reference to FIG. The same code | symbol is attached | subjected about the same structure as 1st Embodiment among the structures of 2nd Embodiment.
 溶解装置1001は、流路1002を画定する内周面1003を有する本体1004と、噴射部1005と、液体供給部7と、分散部8と、を備える。本体1004は、液体に処理剤が分散又は溶解する分散又は溶解部1040と、供給部材11と分散又は溶解部1040とを連結する連結部1041とを有する。 The dissolution apparatus 1001 includes a main body 1004 having an inner peripheral surface 1003 that defines a flow path 1002, an injection unit 1005, a liquid supply unit 7, and a dispersion unit 8. The main body 1004 includes a dispersion or dissolution part 1040 in which the treatment agent is dispersed or dissolved in the liquid, and a connection part 1041 that connects the supply member 11 and the dispersion or dissolution part 1040.
 流路1002は、第1区間1024、第1区間1024よりも一端1020側に位置する第2区間1025、及び、第1区間1024よりも他端1023側に位置する第3区間1026を有する。流路1002において、第1区間1024の流路断面積が最も小さい。 The flow path 1002 includes a first section 1024, a second section 1025 located on the one end 1020 side of the first section 1024, and a third section 1026 located on the other end 1023 side of the first section 1024. In the channel 1002, the channel cross-sectional area of the first section 1024 is the smallest.
 本実施形態の噴射部1005は、流路1002の中心軸αを通る一つの位置(一つの貫通孔)から、流路1002内の一端1020から他端1023に向かう方向に、液体を噴射する。即ち、本実施形態の噴射部1005による液体の噴射方向は、粉体状の処理剤の流れる方向と同じである。また、本実施形態の貫通孔は、流路1002の中心軸α付近に位置している。 The ejection unit 1005 of the present embodiment ejects liquid from one position (one through hole) passing through the central axis α of the flow channel 1002 in a direction from one end 1020 to the other end 1023 in the flow channel 1002. That is, the liquid ejection direction by the ejection unit 1005 of the present embodiment is the same as the flow direction of the powdery processing agent. In addition, the through hole of the present embodiment is located near the central axis α of the flow path 1002.
 本実施形態の噴射部1005は、一つの噴射孔と連通し且つ断面が円状の第1部位1050と、第1部位1050と連通し且つ断面が円状の第2部位1051と、第2部位1051と連通し且つ循環系統10と接続されて液体を供給する第3部位1052と、を有する。本実施形態の第1部位1050及び第2部位1051は、流路1002内に設けられている。 The injection unit 1005 of this embodiment includes a first part 1050 that communicates with one injection hole and has a circular cross section, a second part 1051 that communicates with the first part 1050 and has a circular cross section, and a second part. A third portion 1052 that communicates with 1051 and is connected to the circulation system 10 to supply liquid. The first part 1050 and the second part 1051 of this embodiment are provided in the flow path 1002.
 第3部位1052は、円筒状である。第3部位1052は、第1領域1520と、第1領域1520と接続され本体1004を構成する筒部分の外部に突出した第2領域1521とを含む。本実施形態では、第1領域1520は、本体1004(本実施形態では、連結部1041)と一体的に形成されている。また、第1領域1520は、第2部位1051を囲む第2筒部1053と接続されている。なお、第2筒部1053には、第1部位1050を囲む第1筒部1054が接続されている。 The third portion 1052 has a cylindrical shape. The third portion 1052 includes a first region 1520 and a second region 1521 that is connected to the first region 1520 and protrudes to the outside of the cylindrical portion that constitutes the main body 1004. In the present embodiment, the first region 1520 is formed integrally with the main body 1004 (in the present embodiment, the connecting portion 1041). In addition, the first region 1520 is connected to the second cylindrical portion 1053 that surrounds the second portion 1051. Note that a first tube portion 1054 surrounding the first portion 1050 is connected to the second tube portion 1053.
 第2領域1521を流通する液体は、第1領域1520を通った後、第1部位1050を通って、流路1002内に噴射される。 The liquid flowing through the second region 1521 passes through the first region 1520 and then passes through the first portion 1050 and is injected into the flow path 1002.
 第1筒部1054の内径、及び、流路1002における第1区間1024の流路断面積は、エジェクター効果が有効に機能するように設定される。 The inner diameter of the first tube portion 1054 and the flow path cross-sectional area of the first section 1024 in the flow path 1002 are set so that the ejector effect functions effectively.
 かかる構成の溶解装置1001においても、内周面1003に囲まれた空間(流路1002)内において、該空間に供給されている粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。しかも、噴射される液体が、流路1002の一端1020から他端1023への速度成分を有することで、粉体状の処理剤が分散又は溶解した液体が他端1023から押し出される。そのため、液体が噴射される位置に、供給された粉体状の処理剤が次々に到達し、この位置で分散又は溶解が順次行われることで、処理剤が効率よく分散又は溶解される。 Also in the melting apparatus 1001 having such a configuration, the liquid is vigorously injected into the powdery processing agent supplied to the space in the space (flow path 1002) surrounded by the inner peripheral surface 1003. The powdery treatment agent is sufficiently dispersed or dissolved in this liquid. In addition, since the liquid to be ejected has a velocity component from one end 1020 to the other end 1023 of the flow path 1002, the liquid in which the powdery processing agent is dispersed or dissolved is pushed out from the other end 1023. Therefore, the supplied powdery processing agent successively reaches the position where the liquid is ejected, and the processing agent is efficiently dispersed or dissolved by sequentially performing dispersion or dissolution at this position.
 第2筒部1053における流路1002の流通方向と反対方向(図4における上方向)に位置する面1055は、該方向に凸であって、滑らかな形状である。そのため、一端1020から供給される粉体状の処理剤が、第2筒部1053の面1055に載ったとしても、滑り落ちやすい。これにより、噴射部1005が、粉体状の処理剤の流れを遮ることを抑えることができる。 The surface 1055 located in the direction opposite to the flow direction of the flow path 1002 in the second cylinder portion 1053 (the upward direction in FIG. 4) is convex in this direction and has a smooth shape. Therefore, even if the powdery processing agent supplied from the one end 1020 is placed on the surface 1055 of the second cylindrical portion 1053, it is easily slipped off. Thereby, it can suppress that the injection part 1005 obstruct | occludes the flow of a powdery processing agent.
 なお、本発明にかかる溶解装置1は、上記実施形態の構成に限定されるものではなく、本発明の要旨を逸脱しない範囲で種々の変更が可能である。 The melting apparatus 1 according to the present invention is not limited to the configuration of the above embodiment, and various modifications can be made without departing from the gist of the present invention.
 上記実施形態では、流路2において、第1区間22よりも他端21側に位置する第3区間24の流路断面積が、第1区間22の流路断面積よりも大きかったが、第3区間24の流路断面積が、第1区間22の流路断面積よりも小さくてもよいし、第1区間22の流路断面積と等しくてもよい。この場合であっても、噴射部5から噴射された液体によるエジェクター効果により負圧が生じるため、この処理剤は、流路2の他端21側に吸い込まれ、液体と混ざる。そのため、液体に処理剤を十分に分散又は溶解させることができる。 In the above embodiment, in the flow path 2, the flow path cross-sectional area of the third section 24 located closer to the other end 21 than the first section 22 is larger than the flow path cross-sectional area of the first section 22. The channel cross-sectional area of the three sections 24 may be smaller than the channel cross-sectional area of the first section 22 or may be equal to the channel cross-sectional area of the first section 22. Even in this case, since the negative pressure is generated due to the ejector effect of the liquid ejected from the ejecting section 5, the treatment agent is sucked into the other end 21 side of the flow path 2 and mixed with the liquid. Therefore, the treatment agent can be sufficiently dispersed or dissolved in the liquid.
 また、この場合、第1区間22よりも一端20側に位置する第2区間23の流路断面積が、第1区間22の流路断面積よりも大きく、且つ、噴射部5が液体を流路断面積の小さい第1区間22に噴射していれば、液体を流路断面積の大きい第2区間23に噴射する場合よりも、処理剤と接触しやすい。これにより、処理剤とこの液体とがより混ざりやすくなり、液体に処理剤をより十分に分散又は溶解させることができる。 In this case, the flow path cross-sectional area of the second section 23 located on the one end 20 side of the first section 22 is larger than the flow path cross-sectional area of the first section 22, and the ejection unit 5 flows the liquid. If it injects to the 1st area 22 with a small channel cross-sectional area, it will be easy to contact a processing agent rather than the case where the liquid is injected to the 2nd area 23 with a large channel cross-sectional area. Thereby, a processing agent and this liquid become easier to mix, and a processing agent can be more fully disperse | distributed or dissolved in a liquid.
 さらに、流路2の流路断面積が流路2の中心軸α方向の各位置において均一、即ち、流路2が円柱状の流路であったとしても、内周面3に囲まれた空間(流路2)内において、該空間に供給されている粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。 Furthermore, the cross-sectional area of the flow path 2 is uniform at each position in the direction of the central axis α of the flow path 2, that is, even if the flow path 2 is a cylindrical flow path, it is surrounded by the inner peripheral surface 3. In the space (flow channel 2), the liquid processing agent is sufficiently dispersed or dissolved in the liquid by vigorously ejecting the liquid to the powder processing agent supplied to the space. .
 上記実施形態では、流路2の断面は、円状であったが、楕円状、多角形状等その他の形状であってもよい。断面が楕円状や多角形状である場合、流路の中心軸は、断面の重心を通る軸とする。 In the above embodiment, the flow path 2 has a circular cross section, but may have other shapes such as an ellipse or a polygon. When the cross section is elliptical or polygonal, the central axis of the flow path is an axis passing through the center of gravity of the cross section.
 上記実施形態では、流路2が直線状であったが、一部が曲線状であってもよいし、全体的に曲線状であってもよい。この場合であっても、流路2が直線状でなくても、内周面3に囲まれた空間(流路2)内において、該空間に供給されている粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。 In the above embodiment, the flow path 2 is linear, but a part of the flow path 2 may be curved or may be entirely curved. Even in this case, even if the flow path 2 is not linear, in the space (flow path 2) surrounded by the inner peripheral surface 3, the powdery treatment agent supplied to the space When the liquid is jetted vigorously, the powdery treatment agent is sufficiently dispersed or dissolved in the liquid.
 なお、第2実施形態のように、流路1002の内側に噴射部1005が存在する場合は、流路1002の形状に対応させて、噴射部1005を囲む第1筒部1054及び第2筒部1053を曲げてもよい。即ち、流路1002の曲がった部分に配置される噴射部1005を囲む筒部を、部分的、又は、全体的に曲げてもよく、この場合であっても、粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。 In addition, when the injection part 1005 exists inside the flow path 1002 like 2nd Embodiment, the 1st cylinder part 1054 and the 2nd cylinder part which surround the injection part 1005 corresponding to the shape of the flow path 1002. 1053 may be bent. That is, the cylindrical portion surrounding the injection portion 1005 disposed in the bent portion of the flow path 1002 may be partially or wholly bent, and even in this case, When the liquid is jetted vigorously, the powdery treatment agent is sufficiently dispersed or dissolved in the liquid.
 上記実施形態では、本体4における溶解部40と連結部41とが一体的に形成されているため、液体供給部7を流路2の他端21に近づけて配置することにより、溶解装置の小型化を図ることができる。しかしながら、これに限らず、本体4がそれぞれ個別に形成された溶解部と連結部とを有していてもよい。なお、液体供給部7は、流路2を区画する内周面3が、流路2の中心軸αに対して傾斜している部分に配置されてもよい。 In the above embodiment, since the dissolution part 40 and the connection part 41 in the main body 4 are integrally formed, the liquid supply part 7 is arranged close to the other end 21 of the flow path 2, thereby reducing the size of the dissolution apparatus. Can be achieved. However, the present invention is not limited to this, and the main body 4 may have a dissolving portion and a connecting portion formed individually. The liquid supply unit 7 may be disposed at a portion where the inner peripheral surface 3 that defines the flow channel 2 is inclined with respect to the central axis α of the flow channel 2.
 上記実施形態では、噴射部5において、複数の噴射孔は、周方向に等間隔をあけて設けられているが、異なる間隔をあけて設けられていてもよい。また、第1領域510それぞれの流路断面積は等しく、第2領域520それぞれの流路断面積は等しいため、四つの噴射位置から噴射される液体の量は等しかったが、第1領域510の流路断面積や第2領域520の流路断面積をばらつかせることにより、四つの噴射位置から噴射される液体の量をばらつかせてもよい。 In the above embodiment, in the injection unit 5, the plurality of injection holes are provided at equal intervals in the circumferential direction, but may be provided at different intervals. In addition, since the channel cross-sectional areas of the first regions 510 are equal and the channel cross-sectional areas of the second regions 520 are equal, the amounts of liquid ejected from the four ejection positions were equal. The amount of liquid ejected from the four ejection positions may be varied by varying the channel cross-sectional area and the channel cross-sectional area of the second region 520.
 上記実施形態では、第1実施形態において噴射孔が内周面3に位置し、第2実施形態において噴射孔が流路1002の中心軸α付近に位置していたが、噴射孔が内周面及び流路の中心軸付近の両方に位置していてもよい。 In the above embodiment, the injection hole is located on the inner peripheral surface 3 in the first embodiment, and the injection hole is located near the central axis α of the flow path 1002 in the second embodiment. And near the central axis of the flow path.
 上記実施形態では、流路2の中心軸α方向において、四つの噴射孔のそれぞれは、流路2の他端21と等しい距離だけ離れて設けられている。しかしながら、噴射部5において、この距離は均一でなくてもよい。この場合、噴射部が、噴射部による液体の噴射方向βと流路2の中心軸αとの間の角度を四つの噴射孔において異なるように設計されることで、複数の噴射孔について、液体の噴射方向の交差位置を一点にすることができる。 In the above embodiment, in the direction of the central axis α of the flow path 2, each of the four injection holes is provided at a distance equal to the other end 21 of the flow path 2. However, in the injection unit 5, this distance may not be uniform. In this case, the jetting unit is designed so that the angle between the jetting direction β of the liquid by the jetting unit and the central axis α of the flow path 2 is different in the four jetting holes. The crossing position in the injection direction can be made one point.
 上記実施形態では、一端20から供給された粉体状の処理剤は、流路2内を水平方向に移動せず一端20から他端21に向かう方向に直線的に移動していたが、粉体状の処理剤は、流路2内を周方向に回転しつつ(渦を巻くように移動しつつ)一端20から他端21に向かう方向に移動してもよい。 In the above embodiment, the powdery treatment agent supplied from the one end 20 has moved linearly in the direction from the one end 20 to the other end 21 without moving in the flow path 2 in the horizontal direction. The body-like treatment agent may move in the direction from the one end 20 toward the other end 21 while rotating in the flow path 2 in the circumferential direction (moving so as to spiral).
 上記実施形態では、液体供給部7に、循環系統10から液体が供給されているが、液体供給部7に循環系統10とは異なる場所(例えば、外部)から液体が供給されていてもよい。この場合、液体供給部7に、処理剤が混ざっておらず、且つ、処理剤を分散又は溶解可能な液体、例えば、水を供給してもよい。このように、液体供給部7から内周面3に水を流せば、予め処理剤が混ざった液体を流すよりも、内周面3に付着した処理剤をより分散又は溶解させやすく、処理剤の内周面3への付着をさらに防ぐことができる。また、上記実施形態では、液体供給部7は流路2の中心軸αに対して偏心した位置に配されていたが、これに限らず、中心軸α上に位置するように配されてもよい。 In the above embodiment, the liquid supply unit 7 is supplied with the liquid from the circulation system 10, but the liquid supply unit 7 may be supplied with a liquid from a location (for example, outside) different from the circulation system 10. In this case, the liquid supply unit 7 may be supplied with a liquid that is not mixed with the treatment agent and that can disperse or dissolve the treatment agent, for example, water. In this way, if water is allowed to flow from the liquid supply unit 7 to the inner peripheral surface 3, it is easier to disperse or dissolve the processing agent attached to the inner peripheral surface 3 than to flow a liquid mixed with the processing agent in advance. Can be further prevented from adhering to the inner peripheral surface 3. Moreover, in the said embodiment, although the liquid supply part 7 was distribute | arranged to the position eccentric with respect to the center axis | shaft (alpha) of the flow path 2, it may not be restricted to this but may be distribute | arranged so that it may be located on the center axis | shaft (alpha). Good.
 上記実施形態では、第1分散部材81及び第2分散部材82が別部材であったが、これらが一体的に形成されていてもよい。この場合、第1分散部材及び第2分散部材の組み立て時に、第1分散部材及び第2分散部材に設けられる開口の位置合わせを行わずに、溶解装置を組み立てることができるため、この組み立てが容易である。 In the above embodiment, the first dispersion member 81 and the second dispersion member 82 are separate members, but they may be integrally formed. In this case, when the first dispersion member and the second dispersion member are assembled, the melting device can be assembled without aligning the openings provided in the first dispersion member and the second dispersion member. It is.
 上記実施形態では、分散部8が、第1分散部材81及び第2分散部材82という二つの分散部材を有していたが、一つの分散部材を有してもよいし、三つ以上の複数の分散部材を有してもよい。この場合であっても、流路内で湿気により固まった処理剤が、分散部材に接触して粉砕されるため、処理剤と液体とが混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 In the above embodiment, the dispersion unit 8 has the two dispersion members, the first dispersion member 81 and the second dispersion member 82, but may have one dispersion member, or three or more of the plurality of dispersion members. The dispersion member may be included. Even in this case, the treatment agent solidified by moisture in the flow path is crushed in contact with the dispersion member, so that the treatment agent and the liquid are easily mixed, and the treatment agent is further dispersed or dissolved in the liquid. be able to.
 上記実施形態では、開口810,820のそれぞれは、第1分散部材81及び第2分散部材82の厚み方向から視ると円形状であったが、これに限らず、楕円状や多角形状であってもよい。また、第1分散部材及び第2分散部材において、互いに重ならない位置にスリットが設けられてもよい。さらに、分散部8が、第1分散部材及び第2分散部材を配置した状態で、互いに網目部分が重なることが無いネット状の第1分散部材及び第2分散部材を有してもよい。このような場合であっても、流路内で湿気により固まった処理剤が、分散部材に接触して粉砕されるため、処理剤と液体とが混ざりやすくなり、液体に処理剤をさらに分散又は溶解させることができる。 In the above embodiment, each of the openings 810 and 820 has a circular shape when viewed from the thickness direction of the first dispersion member 81 and the second dispersion member 82. However, the present invention is not limited to this, and the openings 810 and 820 have an elliptical shape or a polygonal shape. May be. In the first dispersion member and the second dispersion member, slits may be provided at positions that do not overlap each other. Furthermore, the dispersion part 8 may have a net-like first dispersion member and second dispersion member in which the mesh portions do not overlap each other in a state where the first dispersion member and the second dispersion member are arranged. Even in such a case, the treatment agent solidified by moisture in the flow path is crushed in contact with the dispersion member, so that the treatment agent and the liquid are easily mixed, and the treatment agent is further dispersed or dispersed in the liquid. Can be dissolved.
 上記実施形態では、溶解装置1は液体供給部7、分散部8を備えていたが、これらの一部及び全部を備えていなくてもよい。この場合であっても、内周面3に囲まれた空間(流路2)内において、該空間に供給されている粉体状の処理剤に、液体が勢いよく噴射されることで、粉体状の処理剤がこの液体に十分に分散又は溶解する。 In the above embodiment, the dissolution apparatus 1 includes the liquid supply unit 7 and the dispersion unit 8, but may not include some or all of them. Even in this case, in the space (flow path 2) surrounded by the inner peripheral surface 3, the liquid is vigorously injected into the powdery processing agent supplied to the space, so that the powder The body treatment agent is sufficiently dispersed or dissolved in the liquid.
 また、溶解装置1の本体4、液体供給部7、及び分散部8は一体的に形成されていても、少なくとも一部が別体で形成されていてもよい。 Further, the main body 4, the liquid supply unit 7, and the dispersion unit 8 of the dissolution apparatus 1 may be formed integrally or at least a part thereof may be formed separately.
 上記実施形態では、溶解装置1が、移送管104~108を介して循環系統10に接続されていたが、溶解装置1が循環系統10に直接接続されていてもよい。この場合、移送管104~108が必要無いため、処理装置100の小型化を図ることができる。 In the above embodiment, the dissolving device 1 is connected to the circulation system 10 via the transfer pipes 104 to 108, but the dissolving device 1 may be directly connected to the circulation system 10. In this case, since the transfer pipes 104 to 108 are not necessary, the processing apparatus 100 can be downsized.
1…溶解装置、2…流路、3…内周面、4…本体、5…噴射部、10…循環系統、20…一端、21…他端、100…処理装置
 
DESCRIPTION OF SYMBOLS 1 ... Melting apparatus, 2 ... Flow path, 3 ... Inner peripheral surface, 4 ... Main body, 5 ... Injection part, 10 ... Circulation system, 20 ... One end, 21 ... Other end, 100 ... Processing apparatus

Claims (10)

  1.  粉体状であり且つ布帛を処理する処理剤が一端から供給されると共に、染色に用いる液体が循環する循環系統に他端が接続されるよう構成された流路を有する本体と、
     前記染色に用いる液体を前記流路内へ該流路の前記一端から前記他端に向かう速度成分を有する方向に噴射する噴射部と、
    を備える、液流式布帛処理装置用の処理剤溶解装置。
    A main body having a flow path configured to be connected to a circulation system in which a treatment agent for treating a fabric is supplied from one end and is in powder form and in which a liquid used for dyeing circulates;
    An ejection unit that ejects the liquid used for the staining into the flow path in a direction having a velocity component from the one end of the flow path toward the other end;
    A processing agent dissolving apparatus for a liquid flow type fabric processing apparatus.
  2.  前記流路は、第1区間、及び、該第1区間よりも前記一端側に位置する第2区間を有し、
     前記第1区間の流路断面積は、前記第2区間の流路断面積よりも小さく、
     前記噴射部は、前記第1区間に向けて、前記染色に用いる液体を噴射する、請求項1に記載の液流式布帛処理装置用の処理剤溶解装置。
    The flow path has a first section and a second section located on the one end side of the first section,
    The channel cross-sectional area of the first section is smaller than the channel cross-sectional area of the second section,
    The treatment agent dissolving apparatus for a liquid flow type fabric treatment apparatus according to claim 1, wherein the ejection unit ejects a liquid used for the dyeing toward the first section.
  3.  前記流路は、前記第1区間よりも前記他端側に位置する第3区間を有し、
     前記第3区間の流路断面積は、前記第1区間の流路断面積よりも大きい、請求項2に記載の液流式布帛処理装置用の処理剤溶解装置。
    The flow path has a third section located on the other end side than the first section,
    The processing agent dissolving apparatus for a liquid flow type fabric processing apparatus according to claim 2, wherein the flow path cross-sectional area of the third section is larger than the flow path cross-sectional area of the first section.
  4.  前記本体は、前記流路を区画する内周面を有し、
     前記染色に用いる液体を、前記内周面に沿って供給する液体供給部を備える、ことを特徴とする請求項1乃至3のいずれか1項に記載の液流式布帛処理装置用の処理剤溶解装置。
    The main body has an inner peripheral surface defining the flow path,
    The processing agent for a liquid-flow-type fabric processing apparatus according to any one of claims 1 to 3, further comprising a liquid supply unit that supplies the liquid used for the dyeing along the inner peripheral surface. Melting device.
  5.  前記液体供給部は、前記内周面の周方向に、前記染色に用いる液体を供給する、ことを特徴とする請求項4に記載の液流式布帛処理装置用の処理剤溶解装置。 The treatment agent dissolving apparatus for a liquid flow type fabric treatment apparatus according to claim 4, wherein the liquid supply section supplies a liquid used for the dyeing in a circumferential direction of the inner peripheral surface.
  6.  前記本体は、前記流路を区画する内周面を有し、
     前記噴射部は、前記内周面から前記流路内に前記染色に用いる液体を噴射する、請求項1乃至3のいずれか1項に記載の液流式布帛処理装置用の処理剤溶解装置。
    The main body has an inner peripheral surface defining the flow path,
    4. The treatment agent dissolving apparatus for a liquid flow type fabric treatment apparatus according to claim 1, wherein the ejection unit ejects a liquid used for the dyeing into the flow path from the inner peripheral surface. 5.
  7.  前記噴射部は、前記内周面における周方向に間隔をあけた複数の位置から、前記流路内に前記染色に用いる液体を噴射する、請求項6に記載の液流式布帛処理装置用の処理剤溶解装置。 The liquid jet type fabric processing apparatus according to claim 6, wherein the spray unit sprays the liquid used for the dyeing into the flow path from a plurality of positions spaced in the circumferential direction on the inner peripheral surface. Treatment agent dissolving device.
  8.  前記流路の前記他端に設けられ、複数の開口を有する第1分散部材
     を備える、請求項1乃至7のいずれか1項に記載の液流式布帛処理装置用の処理剤溶解装置。
    The processing agent dissolution apparatus for a liquid flow type fabric processing apparatus according to any one of claims 1 to 7, further comprising a first dispersion member provided at the other end of the flow path and having a plurality of openings.
  9.  前記流路の流通方向に前記第1分散部材と重ねて、複数の開口を有する第2分散部材が設けられ、
     前記第2分散部材は、該第2分散部材の複数の開口と前記第1分散部材における前記複数の開口とが重ならないように配置される、請求項8に記載の液流式布帛処理装置用の処理剤溶解装置。
    A second dispersion member having a plurality of openings is provided so as to overlap the first dispersion member in the flow direction of the flow path,
    The liquid flow type fabric treatment apparatus according to claim 8, wherein the second dispersion member is disposed so that the plurality of openings of the second dispersion member and the plurality of openings of the first dispersion member do not overlap. Processing agent dissolution equipment.
  10.  請求項1乃至9のいずれか1項に記載の処理剤溶解装置と、
     前記流路の前記一端に向けて、粉体状の処理剤を供給する供給部材と、
     前記染色に用いる液体を循環させて、布帛を処理すると共に、前記流路の前記他端から前記染色に用いる液体が供給される循環系統と、
     を備える、液流式布帛処理装置。
     
    The treatment agent dissolving apparatus according to any one of claims 1 to 9,
    A supply member for supplying a powdery treatment agent toward the one end of the flow path;
    Circulating the liquid used for the dyeing, treating the fabric, and a circulation system for supplying the liquid used for the dyeing from the other end of the flow path;
    A liquid flow type fabric processing apparatus.
PCT/JP2016/075179 2016-08-29 2016-08-29 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus WO2018042486A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
PCT/JP2016/075179 WO2018042486A1 (en) 2016-08-29 2016-08-29 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus
KR1020197005729A KR102503513B1 (en) 2016-08-29 2016-08-29 Treatment agent dissolving device for liquid flow type fabric processing device, and liquid flow type fabric processing device
JP2018536373A JP6843145B2 (en) 2016-08-29 2016-08-29 Treatment agent dissolving device for liquid flow type cloth processing device and liquid flow type cloth processing device
CN201680088832.0A CN109661489B (en) 2016-08-29 2016-08-29 Treating agent dissolving device for liquid flow type fabric treating device, and liquid flow type fabric treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2016/075179 WO2018042486A1 (en) 2016-08-29 2016-08-29 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus

Publications (1)

Publication Number Publication Date
WO2018042486A1 true WO2018042486A1 (en) 2018-03-08

Family

ID=61300516

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2016/075179 WO2018042486A1 (en) 2016-08-29 2016-08-29 Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus

Country Status (4)

Country Link
JP (1) JP6843145B2 (en)
KR (1) KR102503513B1 (en)
CN (1) CN109661489B (en)
WO (1) WO2018042486A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT202100016139A1 (en) * 2021-06-21 2022-12-21 Tecnorama Srl Equipment for producing dye solutions for the textile industry.

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0197265A (en) * 1987-10-05 1989-04-14 Japan Exlan Co Ltd Dyeing liquid automatic preparing apparatus
JPH0952033A (en) * 1995-08-12 1997-02-25 Sakai Erukomu:Kk Automatic cast device for powdery treatment agent
JPH09227838A (en) * 1996-02-19 1997-09-02 Kishimoto Kosakusho:Kk Apparatus for continuously forming stock paste by dissolution
JPH09310270A (en) * 1996-05-22 1997-12-02 Sakai Erukomu:Kk Automatic conveyance of treating powder agent and device used therefor
JPH10102374A (en) * 1996-09-26 1998-04-21 Hisaka Works Ltd Device for dissolving and supplying chemical agent, and chemical agent-charging vessel used therefor
WO2000058543A1 (en) * 1999-03-31 2000-10-05 Termoelettronica S.P.A. Process and device for transporting colouring powders from batching devices to dissolving devices

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3834598A1 (en) * 1988-07-27 1990-02-01 Kleinewefers Ramisch Gmbh DEVICE FOR TREATING A TEXTILE PRODUCT
FR2664506B1 (en) * 1990-07-13 1993-05-07 Bp Chemicals Snc METHOD AND DEVICE FOR INTRODUCING POWDER INTO A REACTOR.
JPH07111024B2 (en) 1993-10-05 1995-11-29 株式会社サカイエルコム Method for directly adding dusting agent to a cloth processing machine, and cloth processing machine used therefor
TW304210B (en) * 1995-08-18 1997-05-01 Sakai Elcom Kk
JP2765817B2 (en) * 1996-02-27 1998-06-18 株式会社日阪製作所 Method for dissolving and supplying powdery drug and apparatus used therefor
CN2561501Y (en) * 2002-08-06 2003-07-23 深圳市清泉水系统工程设备有限公司 Dissolving mixers
JP2009154049A (en) * 2007-12-25 2009-07-16 Kawamura:Kk Liquid mixing apparatus
CN201172742Y (en) * 2008-04-11 2008-12-31 林韦廷 Cloth dyeing machine
CN101412011A (en) * 2008-11-07 2009-04-22 浙江大学 Adjustable spraying apparatus
JP6018838B2 (en) * 2012-08-23 2016-11-02 株式会社加藤製作所 Road sweeper
CN103526479B (en) * 2013-10-21 2016-08-31 江苏海大纺织机械股份有限公司 Colour-spun yarns horizontal Dyeing mould head
CN103861747B (en) * 2014-04-03 2016-07-06 中国药科大学 Trace nozzle
CN204803562U (en) * 2015-05-30 2015-11-25 象山商博电子商务有限公司 Preheat type dyestuff dissolving device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0197265A (en) * 1987-10-05 1989-04-14 Japan Exlan Co Ltd Dyeing liquid automatic preparing apparatus
JPH0952033A (en) * 1995-08-12 1997-02-25 Sakai Erukomu:Kk Automatic cast device for powdery treatment agent
JPH09227838A (en) * 1996-02-19 1997-09-02 Kishimoto Kosakusho:Kk Apparatus for continuously forming stock paste by dissolution
JPH09310270A (en) * 1996-05-22 1997-12-02 Sakai Erukomu:Kk Automatic conveyance of treating powder agent and device used therefor
JPH10102374A (en) * 1996-09-26 1998-04-21 Hisaka Works Ltd Device for dissolving and supplying chemical agent, and chemical agent-charging vessel used therefor
WO2000058543A1 (en) * 1999-03-31 2000-10-05 Termoelettronica S.P.A. Process and device for transporting colouring powders from batching devices to dissolving devices

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT202100016139A1 (en) * 2021-06-21 2022-12-21 Tecnorama Srl Equipment for producing dye solutions for the textile industry.

Also Published As

Publication number Publication date
KR102503513B1 (en) 2023-02-23
KR20190039731A (en) 2019-04-15
CN109661489B (en) 2021-11-02
JPWO2018042486A1 (en) 2019-06-27
JP6843145B2 (en) 2021-03-17
CN109661489A (en) 2019-04-19

Similar Documents

Publication Publication Date Title
CN102212948B (en) Washing machine
US9151032B2 (en) Shower arm for shower WC
KR101148080B1 (en) Apparatus for mixing fluids
KR20130041831A (en) Bubble generator
CN103687987A (en) Washing machine and method for supplying wash water of washing machine
US9475070B2 (en) Water faucet
WO2018042486A1 (en) Treatment agent-dissolving device for liquid flow-type fabric-treatment apparatus and liquid flow-type fabric-treatment apparatus
JP7265952B2 (en) Discharge device and plumbing equipment
JP5423585B2 (en) Drum washing machine
KR101135079B1 (en) Device for desolving gas into water
KR100681931B1 (en) The device and construction of fruit which utilizes water pressure
CN110199059A (en) Laundry treatment appliance with deflecting element
JP2011240477A (en) Water-jet cutting apparatus
JP5291176B2 (en) Mixed spray device for waterproofing materials
JP4373398B2 (en) Injection disperser
JP2016187799A (en) Powder blender and powder blending method
US20190085496A1 (en) Extraction device for extracting a detergent from a dispensing compartment of a washing machine
KR20190051390A (en) Nozzle assembly for mixing fluid
US20220240747A1 (en) Bubble generation apparatus and washing device
JP2017214763A (en) shower head
JP6814381B2 (en) Water spouting device
KR100946818B1 (en) Monolithic injection apparatus for steam injection type washing machine, steam injection type washing machine having the same and install method thereof
KR20150115624A (en) Apparatus for generating plasma
JP2020045768A (en) Ejector
JPH0627679Y2 (en) Powder feeder

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16915047

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2018536373

Country of ref document: JP

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: 20197005729

Country of ref document: KR

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 16915047

Country of ref document: EP

Kind code of ref document: A1