WO2020022019A1 - Processing method and processing device - Google Patents

Processing method and processing device Download PDF

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Publication number
WO2020022019A1
WO2020022019A1 PCT/JP2019/026629 JP2019026629W WO2020022019A1 WO 2020022019 A1 WO2020022019 A1 WO 2020022019A1 JP 2019026629 W JP2019026629 W JP 2019026629W WO 2020022019 A1 WO2020022019 A1 WO 2020022019A1
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WO
WIPO (PCT)
Prior art keywords
container
solid
developing
liquid
solution
Prior art date
Application number
PCT/JP2019/026629
Other languages
French (fr)
Japanese (ja)
Inventor
年宏 渡辺
Original Assignee
富士フイルム株式会社
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 富士フイルム株式会社 filed Critical 富士フイルム株式会社
Publication of WO2020022019A1 publication Critical patent/WO2020022019A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/04Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/06Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of cylindrical shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/04Periodical feeding or discharging; Control arrangements therefor
    • B04B11/05Base discharge
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/38Treatment of water, waste water, or sewage by centrifugal separation
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03FPHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
    • G03F7/00Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
    • G03F7/26Processing photosensitive materials; Apparatus therefor
    • G03F7/40Treatment after imagewise removal, e.g. baking

Definitions

  • the present invention relates to a method and an apparatus for processing a developing fatigue solution, and particularly includes a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution.
  • the present invention relates to a processing method and a processing apparatus for developing fatigue liquid.
  • Various methods are known as a method of developing a printing plate using a photosensitive resin plate.
  • a developing method in which development is performed using an aqueous developing solution containing water as a main component, the photosensitive resin plate after imagewise exposure is immersed in the aqueous developing solution, and an unexposed portion is exposed in the aqueous developing solution with a brush or the like.
  • the development is performed by washing out the uncured resin or the like.
  • the uncured resin or the like exists in a dispersed state in the developer. It has been proposed to remove and reuse the dispersed uncured resin from a developer in which the uncured resin or the like exists in a dispersed state.
  • the above-mentioned developing solution is also called a washing solution.
  • Patent Literature 1 discloses a method of treating a washing liquid containing solid matter generated when developing by removing an unexposed portion while immersing in a washing liquid after exposing a photosensitive resin plate. ing.
  • a treated liquid obtained by separating and removing a solid substance having a specific gravity smaller than that of the washing liquid by using a centrifugal sedimentation type centrifugal separation process having an inside disk, and separating and removing a solid substance having a specific gravity smaller than that of the washing liquid. Is further reused as a washing solution.
  • Patent Document 1 a solid substance having a specific gravity smaller than that of the washing liquid is separated and removed by a centrifugal sedimentation type centrifugal separation process having an inside disk.
  • Patent Document 1 since the separated washing liquid is collected by a skimming tube, a large amount of solid matter is mixed in the washing liquid due to a change in the amount of separated solid matter due to the concentration of solid matter mixed therein. As a result, the solid content of the treated washing liquid increases.
  • Patent Literature 1 In recent years, a flexo plate material compatible with CTP (Computer To Plate) having a black layer layer applied on the surface thereof has appeared, and there is an increasing demand to simultaneously separate solids having a higher specific gravity than the washing liquid from the washing liquid. .
  • CTP Computer To Plate
  • Patent Literature 1 it is possible to separate both a solid substance having a higher specific gravity than the washing liquid and a solid substance having a lower specific gravity than the washing liquid.
  • the captured solid dispersion must be removed after stopping rotation for centrifugation in the case of a batch type.
  • scraper There are two ways to remove the scraper: (i) a method of removing it with a spatula or the like by hand, (ii) a method of installing a scraper in a centrifuge, inserting the scraper inside the rotor while rotating at a low speed, and scraping (iii). There is a method in which a bag-like article or a molded article is provided inside the rotor, and the interior article is taken out.
  • Patent Document 1 it is not possible to extract only the washing liquid by any of the above methods (i) to (iii). For this reason, when removing both the solid matter having a higher specific gravity than the washing liquid and the solid matter having a lower specific gravity than the washing liquid, a large amount of the washing liquid is mixed to increase the water content, and the solid matter is discarded. In this case, the amount of waste increases. Further, Patent Document 1 describes that the treated washing liquid is reused, but when the water content increases as described above, the amount of the washing liquid that can be reused decreases.
  • the present invention provides a developing fatigue solution containing a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution.
  • a processing method for removing solid matter wherein the container is rotated while supplying the developing fatigue liquid into the container, and the solid matter contained in the developing fatigue liquid is centrifuged. It is an object of the present invention to provide a processing method for stopping the rotation of the container after stopping the rotation of the container for a predetermined time.
  • the present invention provides a developing fatigue solution containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washing solution, the specific gravity of which is higher than that of the washing solution. And a second solid having a specific gravity greater than that of the washing solution.
  • the developing method further comprises: supplying a developing fatigue solution into a rotating container; A first step of centrifuging the first solid and the second solid, accumulating the second solid on an inner wall of the container, and accumulating the first solid on a holding member provided in the container; And stopping the supply of the developing fatigue liquid to the rotating container, and continuing the rotation of the container for a certain period of time, and, in a state where the first solid is held by the holding member, The third step of stopping the rotation, and rotating the container, the container is held by the holding member.
  • 1 solids preferably has a fourth step of removing the retaining member.
  • the present invention provides a container having an opening for storing a developing fatigue solution containing a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution.
  • a regulating member provided to face the portion and retaining the first solid substance in the container; and at least one regulating member provided by centrifugal separation provided in the container and on the side opposite to the opening with respect to the regulating member.
  • a holding member for holding the first solid matter to be performed and the drive unit rotates the container in which the developing fatigue liquid is stored, centrifugally separates the first solid matter, and accumulates the first solid matter on the holding member. Stop supplying the developing fatigue solution to the rotating container and wait for a certain time. During this time, the rotation of the container is continued, and further, after the rotation of the container by the driving unit is stopped while the first solid matter accumulated on the holding member is held by the holding member,
  • the present invention provides a processing apparatus having a control unit for rotating a container.
  • the control unit rotates the container by the drive unit to centrifuge the developing fatigue solution in the container, accumulates the first solid matter on the holding member, and then develops the developing fatigue solution in the container.
  • the liquid is discharged from the container, and then, after the rotation of the container by the driving unit is stopped in a state where the first solid matter accumulated on the holding member is held by the holding member, the container is again removed by the driving unit. Preferably, it is rotated.
  • a removing unit for removing the first solid and the second solid present in the container from the container. It is preferable to have a circulation section for reusing the developing fatigue solution discharged from the container as a washing solution.
  • FIG. 1 is a schematic diagram showing a processing system having a first example of a processing apparatus according to an embodiment of the present invention.
  • FIG. 3 is a schematic diagram illustrating an example of a developing device. It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. It is a schematic plan view showing an example of arrangement of a scraper of a processing unit of an embodiment of the present invention.
  • FIG. 3 is a schematic diagram illustrating an example of a developing device. It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. It is a schematic diagram which shows one process of the
  • FIG. 9 is a schematic plan view illustrating another example of the arrangement of the scrapers of the processing apparatus according to the embodiment of the present invention. It is a schematic diagram which shows the modification of the 1st example of the processing apparatus of embodiment of this invention.
  • FIG. 2 is a schematic diagram illustrating a processing system having a second example of the processing apparatus according to the embodiment of the present invention. It is a schematic diagram showing a processing system having a third example of a processing apparatus according to an embodiment of the present invention. It is a schematic diagram showing a processing system having a fourth example of a processing apparatus according to an embodiment of the present invention.
  • FIG. 2 is a schematic diagram showing a processing system having a processing device for comparison.
  • FIG. 1 is a schematic diagram illustrating a processing system having an example of a processing apparatus according to an embodiment of the present invention
  • FIG. 2 is a schematic diagram illustrating an example of a developing apparatus.
  • the processing system 10 shown in FIG. 1 has a processing device 12 and a developing device 14, and the processing device 12 is connected to the developing device 14.
  • a development fatigue solution containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washing solution is generated.
  • the developing fatigue liquid is supplied from the developing device 14 to the processing device 12 via the pipe 31.
  • the processing apparatus 12 is configured such that the first solid matter 36 having a lower specific gravity than the washing liquid contained in the developing fatigue liquid Qw and the second solid substance having a higher specific gravity than the washing liquid are contained in the rotating container 20 for the developing fatigue liquid Qw.
  • the solid 37 is centrifuged. The separated first solids 36 (see FIG. 3) and second solids 37 (see FIG. 3) are removed from the container 20.
  • the processing apparatus 12 performs, for example, centrifugal sedimentation-type centrifugation, and includes a container 20, an inside disk 22, a keeper disk 23, a case 24, a driving unit 26, a pump 29, and a removing unit 33. And a control unit 38.
  • the drive unit 26 and the pump 29 are connected to a control unit 38, and the control unit 38 controls the operations of the drive unit 26 and the pump 29.
  • the operation of the removing unit 33 is also controlled by the control unit 38.
  • the container 20 stores the developing fatigue liquid Qw, and is formed by integrating a cylindrical body 20a, a truncated cone-shaped inclined portion 20b, and a cylindrical bottom 20c.
  • a lid 21a is provided in an opening 20e of the body 20a.
  • the lid 21a is formed of a member having a circular band shape in plan view, and has an opening 21b.
  • the side with the body 20a is the upper side
  • the side with the bottom 20c is the lower side
  • the opening 21b is disposed on the upper side.
  • a shutter 21c is provided in the opening 20f of the inclined portion 20b.
  • the shutter 21c can be opened and closed, and the inclined portion 20b and the bottom portion 20c are not communicated with each other when the shutter 21c is closed.
  • the drive section 26 is provided with a drive shaft 35a, and the drive shaft 35a is provided with a drive gear 35b.
  • a driven gear 35c is provided around the bottom 20c, and the drive gear 35b and the driven gear 35c are engaged.
  • the driving unit 26 rotates the container 20 about the central axis C as a rotation axis, for example, in the direction R, and the first solid material 36 having a specific gravity smaller than the washing liquid contained in the developing fatigue liquid Qw and the washing liquid.
  • the second solid 37 having a large specific gravity is centrifuged in the container 20.
  • the container 20 also functions as a rotating body.
  • the drive unit 26 is configured by, for example, a motor.
  • the combination of the drive shaft 35a, the drive gear 35b, and the driven gear 35c is not limited as long as the container 20 can be rotated using the drive unit 26, and a combination of a drive shaft, a pulley, and a transmission belt is used. You can also.
  • the required acceleration depends on the size of the solids dispersed in the centrifugal effect G, which is a multiple of the gravitational acceleration, but is required to be 300 G or more when the particle size is 1 ⁇ m or more. In order to achieve a further sufficient removal treatment effect, it is more preferable to be 500 G or more. On the other hand, when the particle size is less than 1 ⁇ m, it is preferably 1000 G or more. For this reason, what can produce the centrifugal effect G mentioned above is used for the drive part 26.
  • the rotation number (rpm (revolution per minute)) and rotation time of the container 20 by the driving unit 26 and the rotation timing of the container 20 are controlled by the control unit 38.
  • the control unit 38 rotates the container 20 in which the developing fatigue liquid Qw is stored by the driving unit 26 to perform centrifugal separation, and accumulates the first solid matter 36 on the keeper disk 23. Then, the supply of the developing fatigue solution Qw to the rotating container 20 is stopped, the rotation of the container 20 is continued for a certain time, and then the first solid matter 36 accumulated on the keeper disk 23 is Then, after the rotation of the container 20 by the driving unit 26 is stopped, the driving unit 26 rotates the container 20 again.
  • the above-mentioned fixed time period is, for example, 10 minutes or less, more preferably 30 seconds to 5 minutes, and further preferably 1 to 3 minutes.
  • the above-mentioned fixed time period is also a time period during which the supply of the developing fatigue liquid Qw is stopped. For example, after the supply of the developing fatigue liquid Qw is stopped, the solid matter of the developing fatigue liquid Qw is removed.
  • the bottom 20c is openable and closable on the bottom surface 20d. As shown in FIG. 5, by opening the shutter 21c and the bottom surface 20d, the solid matter in the container 20 can be discharged to the outside. In this case, for example, the tray 32 (see FIG. 5) is disposed below the bottom surface 20d, and the solid matter in the container 20 is collected.
  • a regulating member is provided inside the container 20 and facing the opening 21b.
  • the regulating member holds the first solid matter 36 in the container 20.
  • the regulating member is, for example, the inside disk 22.
  • At least one holding member is provided in the container 20 and on a side opposite to the opening 21b with respect to the regulating member.
  • the holding member holds the first solids 36 accumulated by centrifugation.
  • the holding member is, for example, a keeper disk 23, and the processing device 12 in FIG. 1 has three keeper disks 23.
  • the inside disk 22 and the three keeper disks 23 are spaced apart from each other and are arranged in an overlapping manner.
  • the inside disk 22 is arranged on the lid 21a side facing the opening 21b, and the three keeper disks 23 are arranged on the opposite side of the inside disk 22 from the opening 21b.
  • the number of the keeper disks 23 is not limited to a plurality, and at least one keeper disk may be provided.
  • the inside disk 22 and the keeper disk 23 are both fixed in the container 20 and are configured to rotate together with the container 20 when the container 20 rotates, but the invention is not limited thereto. If the centrifugal force can be applied to the first solid material 36 held by the keeper disk 23 when the container 20 rotates, the installation state of the inside disk 22 and the keeper disk 23 with respect to the container 20 is particularly limited. Not something.
  • the case 24 covers the container 20 and stores the developing fatigue solution Qw overflowing from the opening 21b of the container 20.
  • the container 20 and the case 24 can communicate with each other via an openable and closable outlet (not shown) provided in the inclined portion 20b of the container 20. Therefore, the developing fatigue liquid Qw in the container 20 can be discharged to the case 24.
  • the case 24 is provided with a discharge path 25 serving as a flow path of the developing fatigue liquid Qw from the case 24 to the defoaming tank 27.
  • the developing fatigue solution Qw in the case 24 passes through the discharge path 25 and is stored in the defoaming tank 27.
  • FIG. 9 is a schematic view illustrating a processing system 10 a having a second example of the processing apparatus according to the embodiment of the present invention
  • a separation film 30 is further provided at a position closer to the developing device 14 than the pump 29.
  • the separation film 30 separates solid matter generated by development.
  • the separation film 30 is not particularly limited as long as the solid matter contained in the developing fatigue solution Qw can be separated, and is appropriately determined according to the size of the solid matter to be separated.
  • the separation membrane 30 is not always necessary, and may be configured not to be provided as in the processing system 10 shown in FIG.
  • the developing fatigue solution Qw stored in the defoaming tank 27 is reused without passing through the separation membrane 30 as the developing fatigue solution Qw. Further, even when the separation membrane 30 is provided, it is not always necessary to pass through the separation membrane 30. As described above, the developing fatigue liquid Qw may be used repeatedly without passing through the separation membrane 30. However, when the developing fatigue liquid Qw is passed through the separation membrane 30, the concentration of the solid matter of the developing fatigue liquid Qw returned to the developing device 14 can be further reduced, and the developing fatigue liquid Qw is repeatedly used. It is preferable because it can be performed.
  • the same components as those of the processing system 10 illustrated in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • the separation membrane 30 be capable of separating a solid having a particle size of 1 ⁇ m or less, for example.
  • a filter having a separation ability of 0.1 ⁇ m is used as the separation membrane 30.
  • the container 20 is provided with a pipe 31 for supplying the developing fatigue liquid Qw into the container 20.
  • the pipe 31 is connected to the developing device 14.
  • the opening 31a of the pipe 31 is disposed between the inside disk 22 and the uppermost keeper disk 23.
  • the position of the opening 31a of the pipe 31 is not particularly limited as long as it is below the inside disk 22.
  • the configuration of the container 20 is not particularly limited as long as the container 20 can store the developing fatigue liquid Qw and does not undergo plastic deformation due to centrifugal force acting during rotation for centrifugation.
  • a container used in a centrifugal separator of a centrifugal sedimentation type can be appropriately used.
  • the container 20 has no hole, that is, the body portion 20a, the inclined portion 20b, and the bottom portion 20c are made of a member without holes.
  • a basket-type rotor is used for the container 20.
  • the capacity of the container 20 is not particularly limited, and is appropriately determined by the amount of the solid matter contained in the developing fatigue solution Qw, the amount of plate making in the developing device 14, and the like.
  • the inside disk 22 is for retaining the first solid material 36 having a specific gravity smaller than that of the washing liquid in the container 20, similarly to the above-described regulating member, and is formed of, for example, a disk having an opening 22a.
  • the inside disk 22 is provided near the opening 21b in the container 20 so that the first solids 36 collected inside the container 20 by centrifugation are not discharged out of the container 20 together with the developing fatigue liquid Qw.
  • Can be The first solids 36 collected inside the container 20 are blocked by the inside disk 22 and captured in the container 20.
  • the developing fatigue liquid Qw passes through the outer edge of the inside disk 22 and overflows from the opening 21b of the container 20 to the case 24.
  • the inside disk 22 is made of metal or resin. It is preferable that the inside disk 22 can be installed without removing the lid 21a. In this case, the inside disk 22 is made of a flexible material such as resin.
  • the keeper disk 23 holds the first solid material 36 that is accumulated when centrifuged similarly to the above-described holding member.
  • the holding member holds the first solid object 36, but the first solid object 36 on the keeper disk 23 is finally removed from the keeper disk 23.
  • the keeper disk 23 be formed of a flat plate on which the first solids 36 are easily deposited and on which the first solids 36 are easily scattered when the container 20 rotates.
  • the keeper disk 23 is formed of a disc having no opening.
  • the keeper disk 23 since the keeper disk 23 only needs to be able to accumulate the first solids 36 and hold the first solids 36, at least during centrifugation, according to the mass of the first solids 36. It is sufficient if there is a member at a position where the components are accumulated. For this reason, the keeper disk 23 may be a disk having an opening as described later.
  • the keeper disk 23 is made of, for example, metal.
  • the keeper disk 23 can be made of the same material as the inside disk 22.
  • the defoaming tank 27 stores the developing fatigue liquid Qw.
  • the developing fatigue liquid Qw is once supplied to the defoaming tank 27 and, after removing bubbles, is returned to the developing device 14 by the pump 29.
  • the configuration of the defoaming tank 27 is not particularly limited as long as it can store the developing fatigue solution Qw.
  • the pump 29 returns the developing fatigue liquid Qw from the defoaming tank 27 to the developing device 14 as described above.
  • the configuration of the pump 29 is not particularly limited as long as it can be returned to the developing device 14.
  • the length of the pipe 28, the difference in height between the defoaming tank 27 and the developing device 14, and the development fatigue liquid Qw Is appropriately determined in accordance with the return amount of.
  • the return timing of the developing fatigue solution Qw stored in the defoaming tank 27 by the pump 29 is controlled by the control unit 38.
  • the pump 29 functions as a circulating unit that reuses the developing fatigue liquid Qw discharged from the container 20 as a washing liquid.
  • the removing unit 33 includes, for example, a scraper 34 and a moving unit (not shown) that moves the scraper 34.
  • the scraper 34 scrapes and removes deposits deposited on the inner wall 20 g of the container 20.
  • the first solid material 36 and the second solid material 37 deposited on the inner wall 20g are removed by the scraper 34.
  • the scraper 34 is formed of, for example, a flat plate that can move along the inner wall 20g.
  • the scraper 34 is fixed in the container 20 during centrifugation, and rotates in the same direction R and at the same speed as the container 20. When removing, the scraper 34 is rotated by the moving unit in a direction r (see FIG. 6) opposite to the direction R in which the container 20 rotates.
  • the keeper disk 23 In the processing device 12, by providing the keeper disk 23, the first solid material 36 is retained on the keeper disk 23 when the developing fatigue liquid Qw is collected, so that the first solid material 36 is mixed into the developing fatigue liquid Qw. And the concentration of the solid matter of the developing fatigue solution Qw discharged from the container 20 can be reduced. For this reason, when the developing fatigue solution Qw is reused as the washing solution Q, even if it is reused repeatedly, an increase in the concentration of the solid matter is suppressed, and as a result, the developing fatigue solution Qw is used as the washing solution more times. , Can be reused. In addition, by providing the keeper disk 23, the keeper disk 23 holds the developing fatigue liquid Qw in addition to the first solid material 36. Thereby, the water content of the first solid material 36 and the second solid material 37 discharged to the outside of the container 20 can be reduced.
  • the developing device 14 develops, for example, a photosensitive resin plate using an aqueous washing solution.
  • the developing device 14 is provided with, for example, a developing tank 40 and a brush 42 as shown in FIG.
  • the brush 42 is provided on the driving member 43.
  • the brush 42 is provided with a supply pipe 44.
  • the supply pipe 44 is connected to a supply section 46.
  • the washing liquid is supplied from the supply unit 46 to the surface 50 a of the photosensitive resin plate 50 from the brush 42 via the supply pipe 44.
  • the driving member 43 is rotated by a driving unit (not shown) while the washing liquid Q is supplied from the brush 42 to the surface 50 a of the photosensitive resin plate 50, and the exposed photosensitive resin plate is The surface 50a of the 50 is rubbed.
  • the uncured portion (not shown) after the exposure is removed from the surface 50a of the photosensitive resin plate 50 and discharged into the washing liquid Q.
  • a state in which the uncured portion (not shown) after the exposure is discharged into the washing liquid Q is referred to as a developing fatigue liquid Qw.
  • the washing-out liquid Q is also included in the developing fatigue liquid Qw.
  • the developing tank 40 is connected to the pipe 31. It is sent out from the pipe 31 as a developing fatigue liquid Qw.
  • the pipe 28 is connected to a supply pipe 44.
  • a valve 47 is provided between the pipe 28 and the supply pipe 44. The opening and closing of the valve 47 controls the communication between the pipe 28 and the supply pipe 44.
  • the valve 47 is closed.
  • the processed developing fatigue liquid Qw is supplied from the supply pipe 44 to the photosensitive resin plate 50 via the pipe 28. In this case, the valve 47 is open.
  • the separation film 30 is provided in the pipe 28 as described above, and the processed development fatigue solution Qw is supplied through the separation film 30. You.
  • the developing system of the developing device 14 is not particularly limited, and may be a batch system or a transport system. Further, the developing device 14 may be configured to spray the washing liquid onto the photosensitive resin plate 50 to remove the unexposed portions, or to immerse the photosensitive resin plate 50 in the washing solution to remove the unexposed portions. It may be in a form.
  • the configuration of the photosensitive resin plate 50 is not particularly limited.
  • the photosensitive resin plate 50 forms a flexographic printing plate used for flexographic printing.
  • the photosensitive resin plate 50 is preferably one that can be developed with an aqueous developer mainly containing water, or one that is called a water-developing type flexographic printing plate precursor.
  • a known flexographic printing plate precursor that can be developed with an aqueous developer can be used, and a CTP (Computer To Plate) -compatible flexographic plate material having a black layer layer coated on the surface may be used.
  • CTP Computer To Plate
  • the container 20 is rotated while supplying the developing fatigue solution Qw into the container 20, and the solid matter contained in the developing fatigue solution Qw is centrifuged. Thereafter, the supply of the developing fatigue solution Qw is stopped, and After the rotation of the container 20 is continued during the time, the rotation of the container 20 is stopped. The container 20 is rotated to remove solid matter held by the keeper disk 23 from the keeper disk 23.
  • the schematic diagrams shown in FIGS. 3 to 5 show a processing method using a processing system having an example of the processing apparatus according to the embodiment of the present invention in the order of steps. In the system 10 shown in FIGS.
  • the same components as those of the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted. 3 and 4, illustration of the scraper 34 is omitted.
  • the surface 50a (see FIG. 2) of the photosensitive resin plate 50 is imagewise exposed, that is, exposed in a specific pattern by an exposure device (not shown).
  • the photosensitive resin plate 50 after the imagewise exposure is transported to the developing device 14, where the brush 42 (see FIG. 2) is used in the washing solution Q in the developing tank 40 (see FIG. 2).
  • the developing fatigue liquid Qw is supplied from the developing device 14 to the container 20 rotated about the central axis C by the driving unit 26 via the pipe 31.
  • the first solid matter 36 and the second solid matter 37 contained in the developing fatigue liquid Qw are centrifuged.
  • the centrifugation the solid matter contained in the developing fatigue solution Qw is separated in the container 20 according to the mass.
  • the first solid material 36 and the second solid material 37 are centrifuged in the container 20 under predetermined centrifugation conditions such as the number of rotations and the rotation time, and as shown in FIG.
  • the objects 37 are accumulated on the inner wall 20g of the container 20, and the first solids 36 are accumulated on the keeper disk 23 provided in the container 20 (first step).
  • most of the developing fatigue liquid Qw in the container 20 overflows from the opening 21b and is stored in the case 24.
  • the developing fatigue solution Qw discharged to the case 24 is stored in the defoaming tank 27 via the discharging path 25.
  • the supply of the developing fatigue solution Qw to the rotating container 20 is stopped, and the rotation of the container 20 by the driving unit 26 is continued for a predetermined time (second step).
  • the first solid material 36 is held by the keeper disk 23.
  • for a certain period of time for example, is 10 minutes or less, more preferably 30 seconds to 5 minutes, and still more preferably 1 to 3 minutes.
  • the supply of the developing fatigue liquid Qw is stopped.
  • the supply of the developing fatigue liquid Qw is stopped.
  • the developing fatigue liquid Qw can be supplied.
  • the rotation of the container 20 by the drive unit 26 is stopped while the first solid material 36 is held by the keeper disk 23 (third step). That is, centrifugation is stopped.
  • the container 20 is rotated by the drive unit 26, and centrifugation is performed again.
  • the first solid material 36 held on the keeper disk 23 is removed from the keeper disk 23 by the centrifugal force acting upon rotation (fourth step).
  • the first solid 36 is blown off and deposited on the inner wall 20 g of the body 20 a of the container 20, but the second solid 37 also exerts a centrifugal force when the container 20 rotates.
  • the container 20 is held on the inner wall 20g of the body 20a of the container 20. Therefore, the first solid matter 36 and the second solid matter 37 are deposited on the inner wall 20g of the body 20a.
  • the first solid matter 36 and the second solid matter 37 are simultaneously removed from the container 20 by removing the deposit on the inner wall 20g. Since the first solids 36 and the second solids 37 are removed, the removed first solids 36 and the second solids 37 have a low moisture content. Therefore, when the first solid material 36 and the second solid material 37 are discarded as solid waste, the amount of waste can be reduced. Further, the supply of the developing fatigue solution Qw supplied to the rotating container 20 is stopped, and after the container 20 is continuously rotated for a certain period of time, the rotation of the container 20 is stopped and the container 20 is rotated. I have. Thereby, the solid-liquid separation property is improved, and the amount of the collected solid can be increased.
  • the developing fatigue solution Qw stored in the defoaming tank 27 is returned to the developing device 14 via the pipe 28 by the pump 29.
  • the separation film 30 is provided in the pipe 28, the solid matter contained in the developing fatigue liquid Qw is removed, and the developing apparatus 14 Is returned to the developing fatigue solution Qw.
  • the development fatigue solution Qw is used as a washing solution Q (see FIG. 2) or a rinsing solution for washing off the residue remaining on the plate surface of the photosensitive resin plate 50 after developing and removing the unexposed portion.
  • the first solid matter 36 and the second solid matter 37 present in the container 20 are removed by the removing unit 33, which will be described with reference to FIG.
  • the shutter 21c is opened at the opening 20f of the inclined portion 20b, and the bottom surface 20d of the bottom portion 20c is opened.
  • the pan 32 is arranged below 20d.
  • the scraper 34 is rotated in the direction r opposite to the direction R in which the container 20 rotates, as shown in FIG.
  • the first solid matter 36 and the second solid matter 37 deposited on the inner wall 20g of the container 20 are scraped off, and the first solid matter 36 and the second solid matter 37 deposited on the inner wall 20g are separated. At the same time, it is removed from the container 20.
  • the first solid matter 36 and the second solid matter 37 are removed at the same time, but the present invention is not limited to this, and they may be removed separately.
  • the centrifugation is stopped, that is, between the third step and the fourth step
  • the second solid substance 37 deposited on the inner wall 20g of the container 20 is removed by the scraper 34 (see FIG. 1).
  • Remove from 20 Thereafter, the container 20 is rotated again (fourth step), the first solid material 36 is removed from the keeper disk 23, and the first solid material 36 is deposited on the inner wall 20 g of the container 20. Thereafter, the first solid matter 36 is removed from the container 20 by a scraper 34 (see FIG. 1).
  • first solid matter 36 and the second solid matter 37 are separately removed as described above, since the developing fatigue liquid Qw is removed from the container 20 in a discharged state, the first solid matter 36 is removed. And the second solid substance 37 are removed in a state where the water content is low. Therefore, when the first solid material 36 and the second solid material 37 are discarded as solid waste, the amount of waste can be reduced.
  • the first solid matter 36 and the second solid matter 37 removed from the container 20 are then provided with a dehydration step to further reduce the water content and to be disposed of when discarded as solid waste. The amount can be reduced.
  • a dehydration step in this case, a vacuum type, a heating type, a pressure type, a centrifugal type, or the like can be used, but it is not limited thereto.
  • the processing apparatus 12 has a configuration in which one scraper 34 is provided as shown in FIG. 6, the present invention is not limited to this.
  • a configuration having two scrapers 34 as shown in FIG. In this case, it is preferable to dispose the scrapers 34 diagonally from the viewpoint of removal efficiency.
  • a configuration in which four scrapers 34 are provided may be employed. In this case, it is preferable from the viewpoint of removal efficiency that the scrapers 34 be arranged at regular intervals with respect to the central axis C, that is, at 90 ° intervals.
  • the scraper 34 is not limited to a flat plate that moves along the inner wall 20g.
  • the scraper 34 is disposed in the container 20, but the present invention is not limited to this.
  • the scraper 34 may be inserted into the container 20 when removing.
  • the removing unit 33 for inserting the scraper 34 into the container 20 may be provided separately from the processing apparatus 12.
  • a means (not shown) for injecting compressed air to the inner wall 20g of the container 20 may be provided, and the compressed air may be ejected simultaneously with or before and after the solid material removing operation of the scraper 34.
  • the keeper disk 60 is, for example, a disk having an opening 60a and a main body 60b.
  • the main body 60b of the keeper disk 60 may be located at a position where the first solids 36 are accumulated by centrifugation.
  • FIG. 8 shows only the container 20. In FIG. 8, the keeper disk 60 is used, but the keeper disk 60 may be replaced with the disk-shaped keeper disk 23 having no opening shown in FIG.
  • a step of reusing the developing fatigue liquid Qw discharged from the container 20 as a washing liquid, or the developing fatigue liquid Qw discharged from the container 20 may be used as a solid generated by development.
  • a separation membrane 30 see FIG. 9 for removing substances and reusing it as a washing solution.
  • FIG. 10 is a schematic diagram showing a processing system having a third example of the processing apparatus according to the embodiment of the present invention.
  • the same components as those in the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • the processing system 10b shown in FIG. 10 stores the developing fatigue liquid Qw discharged from the container 20 and a part of the discharged developing fatigue liquid Qw in the container 20 as compared with the processing system 10 shown in FIG.
  • a storage tank 70 having a return supply unit 74 is provided, and that the developing fatigue solution Qw overflowing from the storage tank 70 is supplied to the defoaming tank 27 via a pipe 75. Is the same as the processing system 10 shown in FIG.
  • the storage tank 70 is provided at a lower part in the case 24.
  • the configuration of the storage tank 70 is not particularly limited as long as it can store the developing fatigue solution Qw.
  • a tubular discharge path 21d is provided in the inclined portion 20b of the container 20, and the developing fatigue liquid Qw is discharged from the discharge path 21d to the storage tank 70.
  • the discharge path is not limited to the discharge path 21d as long as the developer fatigue liquid Qw can be discharged into the storage tank 70.
  • the developing fatigue liquid Qw in the container 20 overflows from the opening 21b of the container 20 during rotation, but is discharged to the storage tank 70 via the discharge path 21d when stopped.
  • the developing fatigue liquid Qw discharged from the discharge passage 21d to the storage tank 70 has a large solid content, the developing fatigue liquid Qw in the storage tank 70 is subjected to the centrifugal separation process again, so that the solid substance is recovered. The amount can be increased, and the solid-liquid separation property is improved.
  • a pipe 71 is provided in the storage tank 70, and the pipe 71 is connected to a pump 72.
  • the pump 72 is provided with a pipe 73 for returning a part of the development fatigue solution Qw in the storage tank 70 to the inside of the container 20.
  • a pipe 73 for returning a part of the development fatigue solution Qw in the storage tank 70 to the inside of the container 20.
  • an opening 73 a of the pipe 73 is arranged between the inside disk 22 and the uppermost keeper disk 23.
  • the position of the opening 73a of the pipe 73 is not particularly limited as long as it is below the inside disk 22.
  • the pump 72 is connected to the control unit 38. The operation of the pump 72 is controlled by the control unit 38, and a part of the developing fatigue solution Qw in the storage tank 70 is returned to the container 20 via the pipe 71 and the pipe 73 by the pump 72.
  • the centrifugal separation process is performed at least once, and then the developing fatigue liquid Qw discharged from the container 20 is removed.
  • the portion is returned to the container 20, and the container 20 is rotated to centrifuge the developing fatigue liquid Qw in the container 20, and the first solid matter 36 (see FIG. 3) is accumulated on the keeper disk 23. Is discharged from the container 20 through the discharge path 21d.
  • the container 20 is rotated again.
  • the first solids 36 are removed from the keeper disk 23, and the first solids 36 are deposited on the inner wall 20 g of the container 20.
  • the first solid matter 36 is removed from the container 20 by the scraper 34 (see FIG. 1).
  • the developing fatigue solution Qw in the storage tank 70 remains in the container 20 including the developing fatigue solution Qw discharged from the container 20 after the centrifugal separation process is performed at least once, for example.
  • a centrifugal separation process is performed together with the developing fatigue solution Qw and the like.
  • FIG. 11 is a schematic diagram showing a processing system having a fourth example of the processing apparatus according to the embodiment of the present invention.
  • the same components as those of the processing system 10c illustrated in FIG. 10 are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • the processing system 10c shown in FIG. 11 is different from the processing system 10b shown in FIG. 10 in that the pipe 31 of the developing device 14 does not supply the developing fatigue liquid Qw into the container 20 but is connected to the defoaming tank 27.
  • a liquid sending section 84 for sending the developing fatigue liquid Qw in the defoaming tank 27 into the container 20.
  • the other configuration is the same as the processing system 10b shown in FIG. .
  • the liquid sending section 84 has a pipe 81 provided in the defoaming tank 27, a pump 82 connected to the pipe 81, and a pipe 83 connected to the pump 82.
  • the pipe 83 for example, the opening 83 a of the pipe 83 is disposed between the inside disk 22 and the uppermost keeper disk 23, similarly to the pipe 31 of the processing system 10 shown in FIG. 1.
  • the position of the opening 83a of the pipe 83 is not particularly limited as long as it is below the inside disk 22.
  • the pump 82 is connected to the control unit 38. The operation of the pump 82 is controlled by the control unit 38, and the developing fatigue liquid Qw in the defoaming tank 27 is sent into the container 20 via the pipes 81 and 83 by the pump 82.
  • the developing fatigue solution Qw is not directly supplied from the developing device 14 to the processing device 12, but is stored in the defoaming tank 27, and is then stored in the container 20 by the liquid sending section 84. It is sent.
  • the processing system 10c there are a system of the defoaming tank 27, the developing device 14, and the defoaming tank 27, and a system of the defoaming tank 27, the processing device 12, and the defoaming tank 27, and these systems are operated independently of each other. be able to. Therefore, the processing device 12 can be operated to remove solid components from the developing fatigue liquid Qw without being affected by the operation cycle of the developing device 14.
  • the processing system 10c has a higher degree of freedom in the operation of the processing device 12 than the processing system 10 illustrated in FIG. 1 and the processing system 10b illustrated in FIG. Note that each of the processing system 10b in FIG. 10 and the processing system 10c in FIG. 11 may have a configuration having the separation membrane 30 shown in FIG.
  • the same processing method as the processing system 10 shown in FIG. 10 shown in FIG. 11 can be removed. Further, in the processing system 10c illustrated in FIG. 11, the same processing method as the processing system 10b illustrated in FIG. 10 described above can be performed, and the centrifugal separation process is performed at least once, and then the development fatigue discharged from the container 20 is reduced. In the processing system 10b shown in FIG. 10, including the liquid Qw, the first solid having a lower specific gravity than the washing liquid and the second solid having a higher specific gravity than the washing liquid can be removed.
  • FIG. 12 is a schematic diagram showing a processing system having a processing device for comparison.
  • the same components as those of the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • the processing system 100 shown in FIG. 12 is different from the processing system 10 shown in FIG. 1 in that the processing device 102 is not provided with the keeper disk 23 (see FIG. 1). It is the same as the processing system 10 shown.
  • the first solids 36 accumulate at a position corresponding to the mass due to the centrifugal force. .
  • the first solids 36 accumulate on the inner surface 104 of the inclined portion 20b.
  • the developing fatigue solution Qw in the container 20 is discharged into the case 24 as in the processing method described above, the developing fatigue solution Qw discharged into the case 24 contains a large amount of the first solid matter 36, There is a concern that the solid content concentration of the fatigue fluid Qw will increase.
  • the amount of deposition on the inner surface 104 of the inclined portion 20b is large, it takes time to remove it.
  • the development fatigue solution to be processed by the processing method of the present invention is a washing solution containing solid matter generated by removing unexposed portions by development using a washing solution, that is, a washing solution containing an uncured resin. If there is, it is not particularly limited. However, a developing fatigue solution containing a conventionally known photosensitive resin composition for forming a general photosensitive resin layer can be treated.
  • the processing method is preferably a processing fatigue developing solution when developed by a laser ablation masking (LAM) method, the uncured resin removed by the development is a photosensitive resin contained in the photosensitive resin composition. It is preferably a conductive resin.
  • such a photosensitive resin composition includes, in addition to the photosensitive resin, for example, a composition containing a polymerization initiator, a polymerizable compound, a polymerization inhibitor, a plasticizer, and the like.
  • the developing fatigue liquid to be processed by the processing method of (1) may contain a polymerization initiator, a polymerizable compound, a polymerization inhibitor, a plasticizer, and the like in addition to the uncured resin.
  • the uncured resin contained in the developing fatigue liquid is a solid generated by removing an unexposed portion.
  • Examples of the uncured resin contained in the developing fatigue liquid include a water-dispersible latex, a rubber component, a polymer component, and an uncrosslinked ethylenically unsaturated compound (polymer).
  • water-dispersible latex examples include polybutadiene latex, natural rubber latex, styrene-butadiene copolymer latex, acrylonitrile-butadiene copolymer latex, polychloroprene latex, polyisoprene latex, polyurethane latex, methyl methacrylate-butadiene copolymer latex, A water-dispersed latex polymer such as a water-dispersed latex such as vinylpyridine copolymer latex, butyl polymer latex, thiochol polymer latex, and acrylate polymer latex, or other components such as acrylic acid or methacrylic acid are added to these polymers.
  • a water-dispersed latex such as vinylpyridine copolymer latex, butyl polymer latex, thiochol polymer latex, and acrylate polymer latex, or other components such as acrylic acid or methacrylic acid are added to these polymers.
  • Examples include a polymer obtained by copolymerization.
  • the rubber component include butadiene rubber, isoprene rubber, styrene-butadiene rubber, acrylonitrile rubber, acrylonitrile butadiene rubber, chloroprene rubber, polyurethane rubber, silicone rubber, butyl rubber, ethylene-propylene rubber, and epichlorohydrin rubber.
  • the polymer component may be hydrophilic or hydrophobic, and specific examples include a polyamide resin, an unsaturated polyester resin, an acrylic resin, a polyurethane resin, a polyester resin, and a polyvinyl alcohol resin.
  • the solid having a lower specific gravity than the washing liquid is, for example, a photosensitive resin such as a rubber component and latex.
  • the solid matter having a higher specific gravity than the washing liquid is, for example, a component of the overcoat layer such as carbon.
  • Examples of the ethylenically unsaturated compound (polymer) include a (meth) acryl-modified polymer having an ethylenically unsaturated bond in a molecule.
  • Examples of the (meth) acryl-modified polymer include (meth) acryl-modified butadiene rubber and (meth) acryl-modified nitrile rubber.
  • “(Meth) acryl” is a notation representing acryl or methacryl
  • “(meth) acrylate” described later is a notation representing acrylate or methacrylate.
  • the uncured resin contained in the developing fatigue liquid is not particularly limited, but is preferably 70% by mass or less, more preferably 35% by mass or less.
  • the polymerization initiator that may be contained in the developing fatigue solution is preferably a photopolymerization initiator.
  • the photopolymerization initiator include, for example, alkylphenones, acetophenones, benzoin ethers, benzophenones, thioxanthones, anthraquinones, benzyls, and biacetyls, among which alkylphenones are preferable. .
  • alkylphenone photopolymerization initiator examples include, for example, 2,2-dimethoxy-1,2-diphenylethan-1-one, 1-hydroxy-cyclohexyl-phenyl-ketone, and 2-hydroxy- 2-methyl-1-phenyl-propan-1-one and the like.
  • the concentration of the polymerization initiator that may be contained in the developing fatigue solution is not particularly limited, but is preferably 2.0% by mass or less, more preferably 1.0% by mass or less.
  • Examples of the polymerizable compound that may be contained in the developing fatigue liquid include an ethylenically unsaturated compound corresponding to a so-called monomer component other than the above-mentioned ethylenically unsaturated compound (polymer).
  • the ethylenically unsaturated compound may be a compound having one ethylenically unsaturated bond or a compound having two or more ethylenically unsaturated bonds.
  • Specific examples of the compound having one ethylenically unsaturated bond include 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, 2-hydroxybutyl (meth) acrylate, and 3-chloro-2.
  • the ethylenically unsaturated compound having two or more ethylenically unsaturated bonds include alkyldiol di (meth) acrylates such as 1,9-nonanediol di (meth) acrylate; diethylene glycol di (meth) acrylate Such as polyethylene glycol di (meth) acrylate; polypropylene glycol di (meth) acrylate such as dipropylene glycol di (meth) acrylate; trimethylolpropane tri (meth) acrylate, pentaerythritol tri (meth) acrylate, and pentaerythritol tetra (meth) acrylate.
  • alkyldiol di (meth) acrylates such as 1,9-nonanediol di (meth) acrylate
  • diethylene glycol di (meth) acrylate Such as polyethylene glycol di (meth) acrylate; polypropylene glycol di (
  • a polyvalent (meth) acrylate obtained by the reaction a polyvalent (meth) acrylate obtained by an addition reaction of an unsaturated epoxy compound such as glycidyl (meth) acrylate and a compound having active hydrogen such as a carboxylic acid or an amine
  • Polyvalent (meth) acrylamides such as methylenebis (meth) acrylamide
  • polyvalent vinyl compounds such as divinylbenzene
  • the concentration of the polymerizable compound that may be contained in the developing fatigue solution is not particularly limited, but is preferably 30.0% by mass or less, more preferably 15.0% by mass or less.
  • polymerization inhibitor which may be contained in the development fatigue solution include, for example, hydroquinone monomethyl ether, p-methoxyphenol, di-t-butyl-p-cresol, pyrogallol, t-butylcatechol, benzoquinone, 4,4'-thiobis (3-methyl-6-t-butylphenol), 2,2'-methylenebis (4-methyl-6-t-butylphenol), cerium N-nitrosophenylhydroxyamine, etc. .
  • the concentration of the polymerization inhibitor that may be contained in the developing fatigue solution is not particularly limited, but is preferably 0.3% by mass or less, more preferably 0.15% by mass or less.
  • liquid rubber examples include liquid polybutadiene, liquid polyisoprene, and rubber modified with maleic acid or an epoxy group.
  • oil examples include paraffin, naphthene and aroma.
  • polyester examples include, for example, adipic acid-based polyester and the like.
  • phosphoric acid compound examples include a phosphoric ester.
  • the concentration of the plasticizer that may be contained in the developing fatigue solution is not particularly limited, but is preferably 30% by mass or less, and more preferably 15% by mass or less.
  • the washing solution contained in the developing fatigue solution is preferably an aqueous washing solution, and may be a solution consisting only of water, or containing a water-soluble compound containing at least 50% by mass of water.
  • Aqueous solution may be used.
  • the compound soluble in water include a surfactant, an acid, and an alkali.
  • the surfactant examples include an anionic surfactant, a nonionic surfactant, a cationic surfactant, and an amphoteric surfactant. Among them, an anionic surfactant is preferable.
  • the anionic surfactant include aliphatic carboxylate such as sodium laurate and sodium oleate; higher alcohol sulfate such as sodium lauryl sulfate, sodium cetyl sulfate and sodium oleyl sulfate; Polyoxyethylene alkyl ether sulfates such as sodium polyoxyethylene lauryl ether sulfate; polyoxyethylene alkyl allyl ether sulfates such as sodium polyoxyethylene octyl phenyl ether sulfate and sodium polyoxyethylene nonyl phenyl ether sulfate; Alkyl sulfonates such as alkyl diphenyl ether disulfonate, sodium dodecyl sulfonate, sodium
  • nonionic surfactant examples include polyoxyethylene alkyl ethers such as polyoxyethylene oleyl ether and polyoxyethylene lauryl ether, and polyoxyethylene nonyl phenyl ether and polyoxyethylene such as polyoxyethylene octyl phenyl ether.
  • Mono- and diesters of fatty acids such as ethylene alkyl phenyl ether, polyoxyethylene polyoxypropylene glycols, polyethylene glycol monostearate or polyethylene glycol monooleate or polyethylene glycol dilaurate with polyethylene glycol, sorbitan monolaurate or sorbitan monooleate Esters of sorbitan with fatty acids such as, polyoxyethylene sorbitan monolaurate or Esters of polyoxyethylene adducts of sorbitan such as oxyethylene sorbitan monocitrate or polyoxyethylene sorbitan trilaurate with fatty acids, esters of fatty acids with sorbite such as sorbit monopartitate or sorbit dilaurate, polyoxy Esters of fatty acids such as ethylene sorbit monostearate or polyoxyethylene sorbite diolate and fatty acids, such as pentaerythritol monostearate, esters of pentaerythritol and fatty acids
  • Esters of fatty acids with glycerin fatty acid alkanolamides such as lauric acid diethanolamide or lauric acid monoethanolamide, lauryl dimethylamine Amine compounds such as side oxides, fatty acid alkanolamines such as stearyldiethanolamine, polyoxyethylene alkylamines, triethanolamine fatty acid esters, phosphates, carbonates, and salt compounds showing alkalinity such as silicates. . These may be used alone or in combination of two or more.
  • cationic surfactant examples include primary, secondary and tertiary amine salts such as monostearyl ammonium chloride, distearyl ammonium chloride and tristearyl ammonium chloride, stearyl trimethylammonium chloride, distearyl dimethyl ammonium.
  • Quaternary ammonium salts such as chloride, stearyldimethylbenzylammonium chloride, alkylpyridinium salts such as N-cetylpyridinium chloride or N-stearylpyridinium chloride, N, N-dialkylmorpholinium salts, fatty acid amide salts of polyethylenepolyamine, aminoethylethanol Acetates of urea compounds of amides of amines and stearic acid, 2-alkyl-1-hydroxyethylimidazolinium chloride Ido, and the like. These may be used alone or in combination of two or more.
  • amphoteric surfactant examples include an amino acid type such as sodium laurylamine propionate, a carboxy betaine type such as lauryl dimethyl betaine or lauryl dihydroxyethyl betaine, and a sulfo acid such as stearyl dimethyl sulfoethylene ammonium ethylene ammonium betaine.
  • an amino acid type such as sodium laurylamine propionate
  • a carboxy betaine type such as lauryl dimethyl betaine or lauryl dihydroxyethyl betaine
  • a sulfo acid such as stearyl dimethyl sulfoethylene ammonium ethylene ammonium betaine.
  • Betaine type, imidazolinium betaine type, restin and the like may be used alone or in combination of two or more.
  • the acid include inorganic or organic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, formic acid, acetic acid, oxalic acid, succinic acid, citric acid, malic acid, maleic acid, and paratoluenesulfonic acid.
  • the alkali include lithium hydroxide, sodium hydroxide, magnesium hydroxide, potassium hydroxide, calcium hydroxide, calcium oxide, sodium carbonate, sodium hydrogen carbonate, calcium carbonate and the like.
  • the present invention is basically configured as described above. As described above, the processing method and the processing apparatus of the present invention have been described in detail. However, the present invention is not limited to the above embodiments, and various improvements or changes may be made without departing from the gist of the present invention. Of course.
  • Example 1 In Example 1, the above-mentioned developing fatigue solution was processed using the processing apparatus having the configuration shown in FIG. In Example 1, the operation of stopping the supply of the developing fatigue solution to the rotating container, continuing the rotation of the container for a certain period of time (3 minutes), and then stopping the rotation of the container was performed. This operation is called a first operation. In addition, a scraper and a compressed air jet were used for removing solid matter in the container. In “2500 rpm 5 L / min" shown in the column of centrifugation in Table 1 below, "2500 rpm” indicates the number of revolutions at the time of centrifugation.
  • “5 L / min (liter / min)” indicates a flow rate at which the developing fatigue solution is sent to the centrifuge.
  • the processing amount shown in Table 1 below indicates how many square meters (m 2 ) of the photosensitive resin plate has been developed, and indicates the total area (m 2 ) of the developed photosensitive resin plate. .
  • Example 2 The second embodiment is different from the first embodiment in that processing is performed using the processing apparatus having the configuration shown in FIG. 10 and that the second operation is performed in addition to the first operation. was the same as in Example 1.
  • the second operation is an operation of returning a part of the developing fatigue liquid in the storage tank to the container while rotating the container, and then performing centrifugal separation together with the developing fatigue liquid stored in the container.
  • the amount of collected solids is obtained by the first operation and the second operation.
  • Comparative Example 1 Comparative Example 1 is different from Example 1 in that a processing apparatus without the keeper disk having the configuration shown in FIG. 12 was used and that the container was not rotated again after centrifugation. Same as Example 1.
  • Comparative Example 2 Comparative Example 2 was the same as Comparative Example 1 except that the processing amount was different from that of Comparative Example 1.
  • Example 1 As shown in Table 1, in Examples 1 and 2, compared with Comparative Examples 1 and 2, the amount of collected solids was large, and the water content of the discharged solids could be reduced. Even when Examples 1 and 2 and Comparative Example 2 having the same treatment amount were compared, Examples 1 and 2 showed a larger amount of collected solids. From Examples 1 and 2, Example 2 was able to recover a larger amount of solids than Example 1 by treating the discharged developer fatigue solution again.

Abstract

Provided are a processing method and a processing device in which there is a large amount of solid matter recovered from an exhausted developing solution and moisture content of discharged solids is low. In the processing method, solid matter is removed from the exhausted developing solution containing solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by developing with a wash-out solution. In the processing method, while exhausted developing solution is supplied into a container, the container is rotated, and solid matter contained in the exhausted developing solution is centrifuged, then the supply of the exhausted developing solution is stopped and the container continues to rotate for a certain period of time, and then the container is stopped from rotating.

Description

処理方法および処理装置Processing method and processing apparatus
 本発明は、現像疲労液の処理方法および処理装置に関し、特に、洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液の処理方法および処理装置に関する。 The present invention relates to a method and an apparatus for processing a developing fatigue solution, and particularly includes a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution. The present invention relates to a processing method and a processing apparatus for developing fatigue liquid.
 感光性樹脂版を用いた印刷版の現像方法としては各種方法が知られている。例えば、水を主成分とする水系現像液を用いて現像を行う現像方法では、水系現像液中に画像様露光後の感光性樹脂版を浸漬し、ブラシ等で水系現像液中に未露光部である未硬化樹脂等を洗い出すことにより現像が行われている。この場合、現像液中に未硬化樹脂等が分散した状態で存在する。未硬化樹脂等が分散した状態で存在する現像液について、分散された未硬化樹脂を除去し、再利用することが提案されている。ここで、上述の現像液は洗い出し液とも呼ばれる。 各種 Various methods are known as a method of developing a printing plate using a photosensitive resin plate. For example, in a developing method in which development is performed using an aqueous developing solution containing water as a main component, the photosensitive resin plate after imagewise exposure is immersed in the aqueous developing solution, and an unexposed portion is exposed in the aqueous developing solution with a brush or the like. The development is performed by washing out the uncured resin or the like. In this case, the uncured resin or the like exists in a dispersed state in the developer. It has been proposed to remove and reuse the dispersed uncured resin from a developer in which the uncured resin or the like exists in a dispersed state. Here, the above-mentioned developing solution is also called a washing solution.
 例えば、特許文献1には、感光性樹脂版を露光後、洗い出し液中に浸漬しながら未露光部を除去して現像する際に発生する固形物を含んだ洗い出し液を処理する方法が記載されている。特許文献1では、洗い出し液よりも比重の小さい固形物を、インサイドディスクを有する遠心沈降型の遠心分離処理を用いて分離除去し、洗い出し液よりも比重の小さい固形物を分離除去した処理済液を、さらに洗い出し液として再使用することが記載されている。 For example, Patent Literature 1 discloses a method of treating a washing liquid containing solid matter generated when developing by removing an unexposed portion while immersing in a washing liquid after exposing a photosensitive resin plate. ing. In Patent Document 1, a treated liquid obtained by separating and removing a solid substance having a specific gravity smaller than that of the washing liquid by using a centrifugal sedimentation type centrifugal separation process having an inside disk, and separating and removing a solid substance having a specific gravity smaller than that of the washing liquid. Is further reused as a washing solution.
特開平7-328620号公報JP-A-7-328620
 特許文献1では、洗い出し液よりも比重の小さい固形物は、インサイドディスクを有する遠心沈降型の遠心分離処理で分離除去している。しかし、特許文献1では、分離した洗い出し液をスキミングチューブで回収するため、固形物の混入濃度による、分離されている固形物の量の変化により、洗い出し液の中に固形物が多く混入した場合、処理済の洗い出し液の固形物濃度が高くなる。 In Patent Document 1, a solid substance having a specific gravity smaller than that of the washing liquid is separated and removed by a centrifugal sedimentation type centrifugal separation process having an inside disk. However, in Patent Document 1, since the separated washing liquid is collected by a skimming tube, a large amount of solid matter is mixed in the washing liquid due to a change in the amount of separated solid matter due to the concentration of solid matter mixed therein. As a result, the solid content of the treated washing liquid increases.
 また、近年、表面にブラックレイヤー層が塗布された、CTP(Computer To Plate)対応のフレキソ版材が登場し、洗い出し液よりも比重の大きい固形物も同時に洗い出し液から分離する要求が高まっている。特許文献1では、洗い出し液よりも比重の大きい固形物、および洗い出し液よりも比重の小さい固形物の両方を分離することが可能である。
 特許文献1では、捕捉された固形分散物は回分式の場合は遠心分離のための回転を止めた後に、取り出す必要がある。取り出す方法としては、(i)手でヘラ等を用いて取り出す方法、(ii)遠心分離機にスクレーパーを設置し、低速で回転させながらローター内部にスクレーパーを挿入し掻き取る方法、および(iii)ローター内部に袋状の物または成型品を内装し、内装物ごと取り出す方法が挙げられる。
In recent years, a flexo plate material compatible with CTP (Computer To Plate) having a black layer layer applied on the surface thereof has appeared, and there is an increasing demand to simultaneously separate solids having a higher specific gravity than the washing liquid from the washing liquid. . In Patent Literature 1, it is possible to separate both a solid substance having a higher specific gravity than the washing liquid and a solid substance having a lower specific gravity than the washing liquid.
In Patent Literature 1, the captured solid dispersion must be removed after stopping rotation for centrifugation in the case of a batch type. There are two ways to remove the scraper: (i) a method of removing it with a spatula or the like by hand, (ii) a method of installing a scraper in a centrifuge, inserting the scraper inside the rotor while rotating at a low speed, and scraping (iii). There is a method in which a bag-like article or a molded article is provided inside the rotor, and the interior article is taken out.
 特許文献1では、上述の(i)~(iii)のいずれの方法でも、洗い出し液だけを抜き取ることができない。このため、洗い出し液よりも比重の大きい固形物と、洗い出し液よりも比重の小さい固形物との両方を除去する際、洗い出し液が多く混入して含水率が高くなり、固体廃棄物として廃棄する際、廃棄量が多くなる。また、特許文献1では処理済みの洗い出し液を再使用することが記載されているが、上述のように含水率が高くなると、再使用できる洗い出し液の量が少なくなる。 In Patent Document 1, it is not possible to extract only the washing liquid by any of the above methods (i) to (iii). For this reason, when removing both the solid matter having a higher specific gravity than the washing liquid and the solid matter having a lower specific gravity than the washing liquid, a large amount of the washing liquid is mixed to increase the water content, and the solid matter is discarded. In this case, the amount of waste increases. Further, Patent Document 1 describes that the treated washing liquid is reused, but when the water content increases as described above, the amount of the washing liquid that can be reused decreases.
 本発明の目的は、現像疲労液からの固形物の回収量が多く、かつ排出した固形物の含水率が少ない処理方法および処理装置を提供することにある。 目的 It is an object of the present invention to provide a processing method and a processing apparatus in which the amount of solids recovered from a developing fatigue solution is large and the water content of the discharged solids is low.
 上述の目的を達成するために、本発明は、洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液について、固形物を除去する処理方法であって、現像疲労液を容器内に供給しながら、容器を回転し、現像疲労液に含まれる固形物を遠心分離し、その後、現像疲労液の供給を停止し、一定時間の間、容器の回転を継続した後、容器の回転を停止する、処理方法を提供するものである。 In order to achieve the above object, the present invention provides a developing fatigue solution containing a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution. Is a processing method for removing solid matter, wherein the container is rotated while supplying the developing fatigue liquid into the container, and the solid matter contained in the developing fatigue liquid is centrifuged. It is an object of the present invention to provide a processing method for stopping the rotation of the container after stopping the rotation of the container for a predetermined time.
 また、本発明は、洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液について、洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを除去する処理方法であって、回転する容器内へ現像疲労液を供給し、現像疲労液に含まれる第1の固形物と第2の固形物とを遠心分離し、第2の固形物を容器の内壁に集積し、第1の固形物を容器内に設けられた保持部材に集積させる第1の工程と、回転する容器への現像疲労液の供給を停止し、一定時間の間、容器の回転を継続する第2の工程と、第1の固形物が保持部材に保持された状態で、容器の回転を停止する第3の工程と、容器を回転させて、保持部材に保持された第1の固形物を、保持部材から取り除く第4の工程とを有することが好ましい。 In addition, the present invention provides a developing fatigue solution containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washing solution, the specific gravity of which is higher than that of the washing solution. And a second solid having a specific gravity greater than that of the washing solution. The developing method further comprises: supplying a developing fatigue solution into a rotating container; A first step of centrifuging the first solid and the second solid, accumulating the second solid on an inner wall of the container, and accumulating the first solid on a holding member provided in the container; And stopping the supply of the developing fatigue liquid to the rotating container, and continuing the rotation of the container for a certain period of time, and, in a state where the first solid is held by the holding member, The third step of stopping the rotation, and rotating the container, the container is held by the holding member. 1 solids preferably has a fourth step of removing the retaining member.
 第4の工程の後に、容器から排出された現像疲労液の一部を容器に戻し、容器を回転させて容器内の現像疲労液を遠心分離し、第1の固形物を保持部材に集積させた後、容器内の現像疲労液を容器内から排出し、次に、保持部材に集積された第1の固形物が保持部材に保持された状態で、容器の回転を停止した後、再度、容器を回転させることが好ましい。
 第4の工程の後に、第1の固形物と第2の固形物とを同時に容器から除去する工程を有することが好ましい。
 容器から排出された現像疲労液を洗い出し液として再使用する工程を有することが好ましい。
After the fourth step, a part of the developing fatigue solution discharged from the container is returned to the container, the container is rotated to centrifuge the developing fatigue solution in the container, and the first solid is accumulated on the holding member. After that, the developing fatigue liquid in the container is drained from the container, and then, while the first solid matter accumulated on the holding member is held by the holding member, the rotation of the container is stopped, and again, Preferably, the container is rotated.
Preferably, after the fourth step, a step of simultaneously removing the first solid and the second solid from the container is provided.
It is preferable to have a step of reusing the developing fatigue solution discharged from the container as a washing solution.
 本発明は、洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液を貯留する、開口部を有する容器と、容器を回転させて洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを容器内で遠心分離させる駆動部と、容器内、かつ開口部に面して設けられ、第1の固形物を容器内に留める規制部材と、容器内、かつ規制部材に対して開口部とは反対側に、少なくとも1つ設けられた、遠心分離により集積される第1の固形物を保持する保持部材とを有し、駆動部により現像疲労液が貯留された容器を回転させて遠心分離し、第1の固形物を保持部材に集積させた後、回転する容器への現像疲労液の供給を停止し、一定時間の間、容器の回転を継続し、さらにその後、保持部材に集積された第1の固形物が保持部材に保持された状態で、駆動部による容器の回転を停止した後、再度、駆動部により容器を回転させる制御部とを有する、処理装置を提供するものである。 The present invention provides a container having an opening for storing a developing fatigue solution containing a solid matter generated by removing an unexposed portion of a photosensitive resin plate after imagewise exposure by development using a washing solution. A drive unit for rotating the container to centrifuge a first solid having a lower specific gravity than the washing liquid and a second solid having a higher specific gravity than the washing liquid in the container; A regulating member provided to face the portion and retaining the first solid substance in the container; and at least one regulating member provided by centrifugal separation provided in the container and on the side opposite to the opening with respect to the regulating member. A holding member for holding the first solid matter to be performed, and the drive unit rotates the container in which the developing fatigue liquid is stored, centrifugally separates the first solid matter, and accumulates the first solid matter on the holding member. Stop supplying the developing fatigue solution to the rotating container and wait for a certain time. During this time, the rotation of the container is continued, and further, after the rotation of the container by the driving unit is stopped while the first solid matter accumulated on the holding member is held by the holding member, The present invention provides a processing apparatus having a control unit for rotating a container.
 容器から排出された現像疲労液を貯留し、かつ排出された現像疲労液の一部を容器に戻す供給部を備える貯留槽を有し、供給部により、容器から排出された現像疲労液の一部を容器に戻した後、制御部は、駆動部により容器を回転させて容器内の現像疲労液を遠心分離し、第1の固形物を保持部材に集積させた後、容器内の現像疲労液を容器内から排出し、次に、保持部材に集積された第1の固形物が保持部材に保持された状態で、駆動部による容器の回転を停止した後、再度、駆動部により容器を回転させることが好ましい。 A storage tank for storing the developing fatigue fluid discharged from the container and returning a part of the discharged developing fatigue fluid to the container; and a supply unit configured to store one part of the developing fatigue fluid discharged from the container. After returning the unit to the container, the control unit rotates the container by the drive unit to centrifuge the developing fatigue solution in the container, accumulates the first solid matter on the holding member, and then develops the developing fatigue solution in the container. The liquid is discharged from the container, and then, after the rotation of the container by the driving unit is stopped in a state where the first solid matter accumulated on the holding member is held by the holding member, the container is again removed by the driving unit. Preferably, it is rotated.
 容器内に存在する第1の固形物および第2の固形物を容器から除去する除去部を有することが好ましい。
 容器から排出された現像疲労液を、洗い出し液として再使用する循環部を有することが好ましい。
It is preferable to have a removing unit for removing the first solid and the second solid present in the container from the container.
It is preferable to have a circulation section for reusing the developing fatigue solution discharged from the container as a washing solution.
 本発明によれば、現像疲労液からの固形物の回収量が多く、かつ排出した固形物の含水率が少ない処理方法および処理装置を提供できる。 According to the present invention, it is possible to provide a processing method and a processing apparatus which recover a large amount of solids from a developing fatigue solution and have a low water content of the discharged solids.
本発明の実施形態の処理装置の第1の例を有する処理システムを示す模式図である。FIG. 1 is a schematic diagram showing a processing system having a first example of a processing apparatus according to an embodiment of the present invention. 現像装置の一例を示す模式図である。FIG. 3 is a schematic diagram illustrating an example of a developing device. 本発明の実施形態の処理装置の第1の例を有する処理システムを用いた処理方法の一工程を示す模式図である。It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. 本発明の実施形態の処理装置の第1の例を有する処理システムを用いた処理方法の一工程を示す模式図である。It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. 本発明の実施形態の処理装置の第1の例を有する処理システムを用いた処理方法の一工程を示す模式図である。It is a schematic diagram which shows one process of the processing method using the processing system which has the 1st example of the processing apparatus of embodiment of this invention. 本発明の実施形態の処理装置のスクレーパーの配置の一例を示す模式的平面図である。It is a schematic plan view showing an example of arrangement of a scraper of a processing unit of an embodiment of the present invention. 本発明の実施形態の処理装置のスクレーパーの配置の他の例を示す模式的平面図である。FIG. 9 is a schematic plan view illustrating another example of the arrangement of the scrapers of the processing apparatus according to the embodiment of the present invention. 本発明の実施形態の処理装置の第1の例の変形例を示す模式図である。It is a schematic diagram which shows the modification of the 1st example of the processing apparatus of embodiment of this invention. 本発明の実施形態の処理装置の第2の例を有する処理システムを示す模式図である。FIG. 2 is a schematic diagram illustrating a processing system having a second example of the processing apparatus according to the embodiment of the present invention. 本発明の実施形態の処理装置の第3の例を有する処理システムを示す模式図である。It is a schematic diagram showing a processing system having a third example of a processing apparatus according to an embodiment of the present invention. 本発明の実施形態の処理装置の第4の例を有する処理システムを示す模式図である。It is a schematic diagram showing a processing system having a fourth example of a processing apparatus according to an embodiment of the present invention. 比較のための処理装置を有する処理システムを示す模式図である。FIG. 2 is a schematic diagram showing a processing system having a processing device for comparison.
 以下に、添付の図面に示す好適実施形態に基づいて、本発明の処理方法および処理装置を詳細に説明する。
 なお、以下に説明する図は、本発明を説明するための例示的なものであり、以下に示す図に本発明が限定されるものではない。
 なお、以下において数値範囲を示す「~」とは両側に記載された数値を含む。例えば、εが数値α~数値βとは、εの範囲は数値αと数値βを含む範囲であり、数学記号で示せばα≦ε≦βである。
 「具体的な数値で表された角度」および「垂直」等の角度は、特に記載がなければ、該当する技術分野で一般的に許容される誤差範囲を含む。
Hereinafter, a processing method and a processing apparatus of the present invention will be described in detail based on preferred embodiments shown in the accompanying drawings.
It should be noted that the drawings described below are exemplary for explaining the present invention, and the present invention is not limited to the drawings shown below.
In the following, “to” indicating a numerical range includes the numerical values described on both sides. For example, when ε is a numerical value α 1 to a numerical value β 2 , the range of ε is a range including the numerical values α 1 and β 2 , and α 1 ≦ ε ≦ β 2 in mathematical symbols.
Unless otherwise specified, angles such as “an angle expressed by a specific numerical value” and “vertical” include an error range generally accepted in the relevant technical field.
 図1は本発明の実施形態の処理装置の一例を有する処理システムを示す模式図であり、図2は現像装置の一例を示す模式図である。
 図1に示す処理システム10は、処理装置12と現像装置14とを有し、処理装置12は現像装置14に接続されている。
FIG. 1 is a schematic diagram illustrating a processing system having an example of a processing apparatus according to an embodiment of the present invention, and FIG. 2 is a schematic diagram illustrating an example of a developing apparatus.
The processing system 10 shown in FIG. 1 has a processing device 12 and a developing device 14, and the processing device 12 is connected to the developing device 14.
 現像装置14にて、洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液が生じる。現像装置14から現像疲労液が、配管31を介して処理装置12に供給される。
 処理装置12は、現像疲労液Qwについて、回転する容器20内で、現像疲労液Qwに含まれる洗い出し液よりも比重の小さい第1の固形物36と、洗い出し液よりも比重の大きい第2の固形物37とを遠心分離する。分離された第1の固形物36(図3参照)と、第2の固形物37(図3参照)とを容器20内から除去する。
 処理装置12は、例えば、遠心沈降型の遠心分離を実施するものであり、容器20と、インサイドディスク22と、キーパーディスク23と、ケース24と、駆動部26と、ポンプ29と、除去部33と、制御部38とを有する。駆動部26とポンプ29とは制御部38に接続されており、制御部38により駆動部26とポンプ29の動作とが制御される。また、除去部33も制御部38により動作が制御される。
In the developing device 14, a development fatigue solution containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washing solution is generated. The developing fatigue liquid is supplied from the developing device 14 to the processing device 12 via the pipe 31.
The processing apparatus 12 is configured such that the first solid matter 36 having a lower specific gravity than the washing liquid contained in the developing fatigue liquid Qw and the second solid substance having a higher specific gravity than the washing liquid are contained in the rotating container 20 for the developing fatigue liquid Qw. The solid 37 is centrifuged. The separated first solids 36 (see FIG. 3) and second solids 37 (see FIG. 3) are removed from the container 20.
The processing apparatus 12 performs, for example, centrifugal sedimentation-type centrifugation, and includes a container 20, an inside disk 22, a keeper disk 23, a case 24, a driving unit 26, a pump 29, and a removing unit 33. And a control unit 38. The drive unit 26 and the pump 29 are connected to a control unit 38, and the control unit 38 controls the operations of the drive unit 26 and the pump 29. The operation of the removing unit 33 is also controlled by the control unit 38.
 容器20は、現像疲労液Qwを貯留するものであり、円筒状の胴部20aと、円錐台状の傾斜部20bと、円筒状の底部20cとが一体になったものである。胴部20aの開口20eに蓋21aが設けられている。蓋21aは、平面視円帯状の部材で構成されており、開口部21bを有する。容器20において、胴部20aがある方が上側であり、底部20cがある方が下側であり、開口部21bは上側に配置されている。 The container 20 stores the developing fatigue liquid Qw, and is formed by integrating a cylindrical body 20a, a truncated cone-shaped inclined portion 20b, and a cylindrical bottom 20c. A lid 21a is provided in an opening 20e of the body 20a. The lid 21a is formed of a member having a circular band shape in plan view, and has an opening 21b. In the container 20, the side with the body 20a is the upper side, the side with the bottom 20c is the lower side, and the opening 21b is disposed on the upper side.
 傾斜部20bの開口部20fにシャッター21cが設けられている。シャッター21cは開閉可能であり、シャッター21cが閉じた状態では傾斜部20bと底部20cとは連通されていない。
 駆動部26には駆動軸35aが設けられており、駆動軸35aに駆動ギア35bが設けられている。底部20cの周囲に従動ギア35cが設けられており、駆動ギア35bと従動ギア35cとがかみ合わされている。駆動部26により駆動軸35aを回転させると駆動ギア35bが回転して従動ギア35cが回転し、容器20が回転する。このように駆動部26で発生させた駆動軸35aの回転を容器20に伝達することができる。駆動部26は、中心軸Cを回転軸として容器20を、例えば、方向Rに回転させて、現像疲労液Qwに含まれる洗い出し液よりも比重の小さい第1の固形物36と、洗い出し液よりも比重の大きい第2の固形物37とを容器20内で遠心分離させる。容器20は回転体として機能するものでもある。駆動部26は、例えば、モータで構成される。駆動部26を用いて容器20を回転させることができれば、駆動軸35aと駆動ギア35bと従動ギア35cとの組合せ限定されるものではなく、駆動軸とプーリーと伝動ベルトとを組み合わせたものを用いることもできる。
A shutter 21c is provided in the opening 20f of the inclined portion 20b. The shutter 21c can be opened and closed, and the inclined portion 20b and the bottom portion 20c are not communicated with each other when the shutter 21c is closed.
The drive section 26 is provided with a drive shaft 35a, and the drive shaft 35a is provided with a drive gear 35b. A driven gear 35c is provided around the bottom 20c, and the drive gear 35b and the driven gear 35c are engaged. When the drive shaft 35a is rotated by the drive unit 26, the drive gear 35b rotates, the driven gear 35c rotates, and the container 20 rotates. Thus, the rotation of the drive shaft 35a generated by the drive unit 26 can be transmitted to the container 20. The driving unit 26 rotates the container 20 about the central axis C as a rotation axis, for example, in the direction R, and the first solid material 36 having a specific gravity smaller than the washing liquid contained in the developing fatigue liquid Qw and the washing liquid. The second solid 37 having a large specific gravity is centrifuged in the container 20. The container 20 also functions as a rotating body. The drive unit 26 is configured by, for example, a motor. The combination of the drive shaft 35a, the drive gear 35b, and the driven gear 35c is not limited as long as the container 20 can be rotated using the drive unit 26, and a combination of a drive shaft, a pulley, and a transmission belt is used. You can also.
 遠心分離において、必要な加速度は、加速度を重力加速度に対する倍数である遠心効果Gで表わすと、分散している固形物の大きさにもよるが、粒径が1μm以上の場合300G以上であることが好ましく、さらに充分な除去処理効果を達成するためには500G以上であることがより好ましい。一方、粒径が1μm未満の時には1000G以上であることが好ましい。このため、駆動部26には、上述の遠心効果Gを生じさせることができるものが用いられる。駆動部26による容器20の回転数(rpm(revolution per minute))および回転時間、ならびに容器20の回転のタイミングは制御部38により制御される。 In centrifugation, the required acceleration depends on the size of the solids dispersed in the centrifugal effect G, which is a multiple of the gravitational acceleration, but is required to be 300 G or more when the particle size is 1 μm or more. In order to achieve a further sufficient removal treatment effect, it is more preferable to be 500 G or more. On the other hand, when the particle size is less than 1 μm, it is preferably 1000 G or more. For this reason, what can produce the centrifugal effect G mentioned above is used for the drive part 26. The rotation number (rpm (revolution per minute)) and rotation time of the container 20 by the driving unit 26 and the rotation timing of the container 20 are controlled by the control unit 38.
 制御部38は、後に説明するが処理方法において、駆動部26により現像疲労液Qwが貯留された容器20を回転させて遠心分離し、第1の固形物36をキーパーディスク23に集積させた後、回転する容器20への現像疲労液Qwの供給を停止し、一定時間の間、容器20の回転を継続し、さらにその後、キーパーディスク23に集積された第1の固形物36がキーパーディスク23に保持された状態で、駆動部26による容器20の回転を停止した後、再度、駆動部26により容器20を回転させる。
 なお、上述の一定時間の間とは、例えば、10分以下であり、より好ましくは30秒~5分であり、更に好ましくは1~3分である。上述の一定時間の間とは、現像疲労液Qwの供給を停止する時間のことでもある。例えば、現像疲労液Qwの供給を停止した後、現像疲労液Qwの固形物が除去される。
In the processing method, which will be described later, the control unit 38 rotates the container 20 in which the developing fatigue liquid Qw is stored by the driving unit 26 to perform centrifugal separation, and accumulates the first solid matter 36 on the keeper disk 23. Then, the supply of the developing fatigue solution Qw to the rotating container 20 is stopped, the rotation of the container 20 is continued for a certain time, and then the first solid matter 36 accumulated on the keeper disk 23 is Then, after the rotation of the container 20 by the driving unit 26 is stopped, the driving unit 26 rotates the container 20 again.
The above-mentioned fixed time period is, for example, 10 minutes or less, more preferably 30 seconds to 5 minutes, and further preferably 1 to 3 minutes. The above-mentioned fixed time period is also a time period during which the supply of the developing fatigue liquid Qw is stopped. For example, after the supply of the developing fatigue liquid Qw is stopped, the solid matter of the developing fatigue liquid Qw is removed.
 詳細には示していないが、底部20cは、底面20dが開閉可能である。図5に示すように、シャッター21cと底面20dを開けることにより、容器20内の固形物を外部に排出させることができる。この場合、例えば、底面20dの下方に受皿32(図5参照)を配置して、容器20内の固形物を回収する。 Although not shown in detail, the bottom 20c is openable and closable on the bottom surface 20d. As shown in FIG. 5, by opening the shutter 21c and the bottom surface 20d, the solid matter in the container 20 can be discharged to the outside. In this case, for example, the tray 32 (see FIG. 5) is disposed below the bottom surface 20d, and the solid matter in the container 20 is collected.
 容器20内、かつ開口部21bに面して規制部材が設けられている。規制部材は第1の固形物36を容器20内に留めるものである。規制部材は、例えば、インサイドディスク22である。
 容器20内、かつ規制部材に対して開口部21bとは反対側に、少なくとも1つ保持部材が設けられている。保持部材は遠心分離により集積される第1の固形物36を保持するものである。保持部材は、例えば、キーパーディスク23であり、図1の処理装置12は、3つのキーパーディスク23を有する。
A regulating member is provided inside the container 20 and facing the opening 21b. The regulating member holds the first solid matter 36 in the container 20. The regulating member is, for example, the inside disk 22.
At least one holding member is provided in the container 20 and on a side opposite to the opening 21b with respect to the regulating member. The holding member holds the first solids 36 accumulated by centrifugation. The holding member is, for example, a keeper disk 23, and the processing device 12 in FIG. 1 has three keeper disks 23.
 インサイドディスク22と、3つのキーパーディスク23とは離間し、かつ重ねて配置されている。
 インサイドディスク22が蓋21a側に開口部21bに面して配置され、3つのキーパーディスク23は、インサイドディスク22に対して開口部21bとは反対側に配置されている。なお、キーパーディスク23は、複数設けることに限定されるものではなく、少なくとも1つあればよい。
 インサイドディスク22とキーパーディスク23とは、いずれも容器20内に固定されていて、容器20の回転した場合、容器20と一緒に回転する構成であるが、これに限定されるものではない。容器20が回転した際に、キーパーディスク23に保持された第1の固形物36に遠心力を作用させることができれば、インサイドディスク22およびキーパーディスク23の、容器20に対する設置状態は、特に限定されるものではない。
The inside disk 22 and the three keeper disks 23 are spaced apart from each other and are arranged in an overlapping manner.
The inside disk 22 is arranged on the lid 21a side facing the opening 21b, and the three keeper disks 23 are arranged on the opposite side of the inside disk 22 from the opening 21b. The number of the keeper disks 23 is not limited to a plurality, and at least one keeper disk may be provided.
The inside disk 22 and the keeper disk 23 are both fixed in the container 20 and are configured to rotate together with the container 20 when the container 20 rotates, but the invention is not limited thereto. If the centrifugal force can be applied to the first solid material 36 held by the keeper disk 23 when the container 20 rotates, the installation state of the inside disk 22 and the keeper disk 23 with respect to the container 20 is particularly limited. Not something.
 ケース24は、容器20を覆うものであり、容器20の開口部21bから溢れ出た現像疲労液Qwを貯留するものである。また、容器20の傾斜部20bに設けられた、開閉可能な排出口(図示せず)により、容器20とケース24とは連通可能である。このため、容器20内の現像疲労液Qwをケース24に排出することができる。
 ケース24には、ケース24から消泡タンク27への現像疲労液Qwの流路となる排出路25が設けられている。ケース24内の現像疲労液Qwは排出路25を通り、消泡タンク27に貯留される。
The case 24 covers the container 20 and stores the developing fatigue solution Qw overflowing from the opening 21b of the container 20. The container 20 and the case 24 can communicate with each other via an openable and closable outlet (not shown) provided in the inclined portion 20b of the container 20. Therefore, the developing fatigue liquid Qw in the container 20 can be discharged to the case 24.
The case 24 is provided with a discharge path 25 serving as a flow path of the developing fatigue liquid Qw from the case 24 to the defoaming tank 27. The developing fatigue solution Qw in the case 24 passes through the discharge path 25 and is stored in the defoaming tank 27.
 消泡タンク27と現像装置14とは配管28で接続されている。配管28にはポンプ29が設けられている。本発明の実施形態の処理装置の第2の例を有する処理システム10aを示す模式図である図9では、さらに、ポンプ29よりも現像装置14に近い位置に分離膜30が設けられている。分離膜30は、現像により発生する固形物を分離するものである。このため、分離膜30は、現像疲労液Qwに含まれる固形物を分離することができれば、特に限定されるものではなく、分離する固形物の大きさにより適宜決定される。なお、分離膜30は、必ずしも必要ではなく、図1に示す処理システム10のように設けない構成でもよい。この場合、現像疲労液Qwは、分離膜30を通過することなく、消泡タンク27に貯留された現像疲労液Qwがそのまま再使用される。また、分離膜30を有する場合でも、分離膜30を必ず通過させる必要はない。このように、分離膜30を通過させることなく、現像疲労液Qwを繰り返し使用してもよい。
 しかしながら、現像疲労液Qwは分離膜30を通過させた方が、現像装置14に返送される現像疲労液Qwの固形物の濃度を、さらに低くすることができ、現像疲労液Qwを繰り返し使用することができるため好ましい。
 なお、図9に示す処理システム10aにおいて、図1に示す処理システム10と同一構成物には同一符号を付して、その詳細な説明は省略する。
The defoaming tank 27 and the developing device 14 are connected by a pipe 28. The pipe 28 is provided with a pump 29. In FIG. 9, which is a schematic view illustrating a processing system 10 a having a second example of the processing apparatus according to the embodiment of the present invention, a separation film 30 is further provided at a position closer to the developing device 14 than the pump 29. The separation film 30 separates solid matter generated by development. For this reason, the separation film 30 is not particularly limited as long as the solid matter contained in the developing fatigue solution Qw can be separated, and is appropriately determined according to the size of the solid matter to be separated. Note that the separation membrane 30 is not always necessary, and may be configured not to be provided as in the processing system 10 shown in FIG. In this case, the developing fatigue solution Qw stored in the defoaming tank 27 is reused without passing through the separation membrane 30 as the developing fatigue solution Qw. Further, even when the separation membrane 30 is provided, it is not always necessary to pass through the separation membrane 30. As described above, the developing fatigue liquid Qw may be used repeatedly without passing through the separation membrane 30.
However, when the developing fatigue liquid Qw is passed through the separation membrane 30, the concentration of the solid matter of the developing fatigue liquid Qw returned to the developing device 14 can be further reduced, and the developing fatigue liquid Qw is repeatedly used. It is preferable because it can be performed.
In the processing system 10a illustrated in FIG. 9, the same components as those of the processing system 10 illustrated in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
 ここで、特許文献1に記載のように、洗い出し液よりも比重の小さい固形物を分離除去した処理済液を、さらに洗い出し液として再使用することについて検証を行ったところ、現像の際、感光性樹脂版へのカス付着が多くなる傾向が見られた。
 分析したところ、洗い出し液よりも比重の小さい固形物には、粒径が1~5μmの成分と粒径が1μm以下の成分があり、粒径が1~5μmの固形物はほとんど分離除去されているが、粒径が1μm以下の成分が徐々に増えていることが判明した。これは、遠心分離装置で除去できる成分は固形物が粒径1~5μmの固形物で、粒径が1μm以下の成分は遠心分離では除去できないため、再使用により濃度が上昇しているためと考えられる。このことから、分離膜30は、例えば、粒径が1μm以下の固形物を分離できるものであることが好ましい。例えば、分離膜30として、分離能が0.1μmのフィルターが用いられる。
Here, as described in Patent Document 1, it was verified that the treated liquid obtained by separating and removing a solid substance having a lower specific gravity than the washing liquid was reused as a washing liquid. There was a tendency that scum adheres to the conductive resin plate.
As a result of analysis, the solid matter having a specific gravity smaller than that of the washing liquid has a component having a particle size of 1 to 5 μm and a component having a particle size of 1 μm or less, and the solid material having a particle size of 1 to 5 μm is almost separated and removed. However, it was found that components having a particle size of 1 μm or less gradually increased. This is because the components that can be removed by the centrifugal separator are solids having a particle size of 1 to 5 μm, and the components having a particle size of 1 μm or less cannot be removed by centrifugation, and the concentration is increased by reuse. Conceivable. For this reason, it is preferable that the separation membrane 30 be capable of separating a solid having a particle size of 1 μm or less, for example. For example, a filter having a separation ability of 0.1 μm is used as the separation membrane 30.
 容器20には、現像疲労液Qwを容器20内に供給する配管31が配置されている。配管31は現像装置14に接続されている。例えば、配管31の開口31aは、インサイドディスク22と、一番上のキーパーディスク23との間に配置されている。配管31の開口31aはインサイドディスク22の下側であれば、その位置は特に限定されるものではない。
 容器20は、内部に現像疲労液Qwを貯留でき、かつ遠心分離のための回転時に作用する遠心力により、塑性変形することがなければ、その構成は特に限定されるものではない。容器20は、例えば、遠心沈降型の遠心分離装置に利用されるものが適宜利用可能である。この場合、容器20は孔がない構成、すなわち、胴部20aと傾斜部20bと底部20cは孔がない部材で構成される。例えば、容器20には、バスケット型ローターが用いられる。
 また、容器20の容量は、特に限定されるものではなく、現像疲労液Qwに含まれる固形物の量、および現像装置14での製版量等により適宜決定されるものである。
The container 20 is provided with a pipe 31 for supplying the developing fatigue liquid Qw into the container 20. The pipe 31 is connected to the developing device 14. For example, the opening 31a of the pipe 31 is disposed between the inside disk 22 and the uppermost keeper disk 23. The position of the opening 31a of the pipe 31 is not particularly limited as long as it is below the inside disk 22.
The configuration of the container 20 is not particularly limited as long as the container 20 can store the developing fatigue liquid Qw and does not undergo plastic deformation due to centrifugal force acting during rotation for centrifugation. As the container 20, for example, a container used in a centrifugal separator of a centrifugal sedimentation type can be appropriately used. In this case, the container 20 has no hole, that is, the body portion 20a, the inclined portion 20b, and the bottom portion 20c are made of a member without holes. For example, a basket-type rotor is used for the container 20.
Further, the capacity of the container 20 is not particularly limited, and is appropriately determined by the amount of the solid matter contained in the developing fatigue solution Qw, the amount of plate making in the developing device 14, and the like.
 インサイドディスク22は、上述の規制部材と同じく洗い出し液よりも比重の小さい第1の固形物36を容器20内に留めるためのものであり、例えば、開口22aを有する円板で構成される。インサイドディスク22は、遠心分離により、容器20の内側に集まった第1の固形物36が現像疲労液Qwと一緒に容器20の外へ排出されないように、容器20内の開口部21b付近に設けられる。
 容器20の内側に集まった第1の固形物36はインサイドディスク22により遮られて容器20内に捕捉される。現像疲労液Qwはインサイドディスク22の外縁側を通過して容器20の開口部21bからケース24に溢れ出る。
The inside disk 22 is for retaining the first solid material 36 having a specific gravity smaller than that of the washing liquid in the container 20, similarly to the above-described regulating member, and is formed of, for example, a disk having an opening 22a. The inside disk 22 is provided near the opening 21b in the container 20 so that the first solids 36 collected inside the container 20 by centrifugation are not discharged out of the container 20 together with the developing fatigue liquid Qw. Can be
The first solids 36 collected inside the container 20 are blocked by the inside disk 22 and captured in the container 20. The developing fatigue liquid Qw passes through the outer edge of the inside disk 22 and overflows from the opening 21b of the container 20 to the case 24.
 インサイドディスク22は金属または樹脂等で構成される。インサイドディスク22は、蓋21aを取り外さずに設置できることが好ましく、この場合、インサイドディスク22は可撓性のあるもので構成され、例えば、樹脂等で構成される。 The inside disk 22 is made of metal or resin. It is preferable that the inside disk 22 can be installed without removing the lid 21a. In this case, the inside disk 22 is made of a flexible material such as resin.
 キーパーディスク23は、上述の保持部材と同じく遠心分離した際に集積される第1の固形物36を保持するものである。容器20内から現像疲労液Qwを排出した場合、キーパーディスク23に集積された第1の固形物36はキーパーディスク23上に保持される。
 保持部材は第1の固形物36を保持するが、最終的にはキーパーディスク23上の第1の固形物36は、キーパーディスク23上から取り除かれる。このことから、キーパーディスク23は、第1の固形物36が堆積されやすく、かつ容器20の回転時に第1の固形物36が飛ばされやすい平板で構成することが好ましい。このため、例えば、キーパーディスク23は開口のない円板で構成される。
The keeper disk 23 holds the first solid material 36 that is accumulated when centrifuged similarly to the above-described holding member. When the developing fatigue liquid Qw is discharged from the container 20, the first solid matter 36 accumulated on the keeper disk 23 is held on the keeper disk 23.
The holding member holds the first solid object 36, but the first solid object 36 on the keeper disk 23 is finally removed from the keeper disk 23. For this reason, it is preferable that the keeper disk 23 be formed of a flat plate on which the first solids 36 are easily deposited and on which the first solids 36 are easily scattered when the container 20 rotates. For this reason, for example, the keeper disk 23 is formed of a disc having no opening.
 しかしながら、キーパーディスク23は、第1の固形物36が集積され、かつ第1の固形物36を保持することができればよいため、少なくとも、遠心分離の際、第1の固形物36の質量に応じて集積される位置に部材があればよい。このため、キーパーディスク23は、後述のように開口を有する円板でもよい。
 キーパーディスク23は、例えば、金属で構成される。キーパーディスク23は、インサイドディスク22と同じ材質とすることもできる。
However, since the keeper disk 23 only needs to be able to accumulate the first solids 36 and hold the first solids 36, at least during centrifugation, according to the mass of the first solids 36. It is sufficient if there is a member at a position where the components are accumulated. For this reason, the keeper disk 23 may be a disk having an opening as described later.
The keeper disk 23 is made of, for example, metal. The keeper disk 23 can be made of the same material as the inside disk 22.
 消泡タンク27は、現像疲労液Qwを貯留するものである。現像疲労液Qwは、一旦消泡タンク27に供給され、泡を抜いた後に、ポンプ29により現像装置14に返送される。消泡タンク27は、現像疲労液Qwを貯留することができれば、その構成は特に限定されるものではない。
 ポンプ29は、上述のように、消泡タンク27の現像疲労液Qwを現像装置14に返送するものである。ポンプ29は、現像装置14に返送することができれば、その構成は特に限定されるものではなく、配管28の長さ、消泡タンク27と現像装置14との高さの差および現像疲労液Qwの返送量に応じて適宜決定されるものである。
 なお、消泡タンク27に貯留された現像疲労液Qwのポンプ29による返送のタイミングは制御部38により制御される。ポンプ29は、容器20から排出された現像疲労液Qwを、洗い出し液として再使用する循環部として機能する。
The defoaming tank 27 stores the developing fatigue liquid Qw. The developing fatigue liquid Qw is once supplied to the defoaming tank 27 and, after removing bubbles, is returned to the developing device 14 by the pump 29. The configuration of the defoaming tank 27 is not particularly limited as long as it can store the developing fatigue solution Qw.
The pump 29 returns the developing fatigue liquid Qw from the defoaming tank 27 to the developing device 14 as described above. The configuration of the pump 29 is not particularly limited as long as it can be returned to the developing device 14. The length of the pipe 28, the difference in height between the defoaming tank 27 and the developing device 14, and the development fatigue liquid Qw Is appropriately determined in accordance with the return amount of.
The return timing of the developing fatigue solution Qw stored in the defoaming tank 27 by the pump 29 is controlled by the control unit 38. The pump 29 functions as a circulating unit that reuses the developing fatigue liquid Qw discharged from the container 20 as a washing liquid.
 除去部33は、例えば、スクレーパー34と、スクレーパー34を移動させる移動部(図示せず)とを有する。スクレーパー34は、容器20の内壁20gに堆積した堆積物を掻き取って除去するものである。スクレーパー34により、内壁20gに堆積した第1の固形物36および第2の固形物37が除去される。
 スクレーパー34は、例えば、内壁20gに沿って移動可能な平板で構成される。スクレーパー34は、遠心分離時には、容器20内に固定された状態にあり、容器20と同じ方向R、かつ同じ速度で回転する。除去する際には、移動部により、スクレーパー34は、容器20が回転する方向Rと反対の方向r(図6参照)に回転される。
The removing unit 33 includes, for example, a scraper 34 and a moving unit (not shown) that moves the scraper 34. The scraper 34 scrapes and removes deposits deposited on the inner wall 20 g of the container 20. The first solid material 36 and the second solid material 37 deposited on the inner wall 20g are removed by the scraper 34.
The scraper 34 is formed of, for example, a flat plate that can move along the inner wall 20g. The scraper 34 is fixed in the container 20 during centrifugation, and rotates in the same direction R and at the same speed as the container 20. When removing, the scraper 34 is rotated by the moving unit in a direction r (see FIG. 6) opposite to the direction R in which the container 20 rotates.
 処理装置12では、キーパーディスク23を設けることにより、現像疲労液Qwの回収時に、キーパーディスク23に第1の固形物36が保持されるため、第1の固形物36が現像疲労液Qwに混入しにくくなり、容器20から排出される現像疲労液Qwの固形物の濃度を低くできる。このため、現像疲労液Qwを洗い出し液Qとして再使用した場合、繰り返し再使用しても、固形物の濃度の上昇が抑制され、結果として、現像疲労液Qwを洗い出し液として、より多くの回数、再使用することができる。
 また、キーパーディスク23を設けることにより、キーパーディスク23に第1の固形物36以外に現像疲労液Qwも保持される。これにより、容器20の外部に排出された、第1の固形物36および第2の固形物37の含水率を低くできる。
In the processing device 12, by providing the keeper disk 23, the first solid material 36 is retained on the keeper disk 23 when the developing fatigue liquid Qw is collected, so that the first solid material 36 is mixed into the developing fatigue liquid Qw. And the concentration of the solid matter of the developing fatigue solution Qw discharged from the container 20 can be reduced. For this reason, when the developing fatigue solution Qw is reused as the washing solution Q, even if it is reused repeatedly, an increase in the concentration of the solid matter is suppressed, and as a result, the developing fatigue solution Qw is used as the washing solution more times. , Can be reused.
In addition, by providing the keeper disk 23, the keeper disk 23 holds the developing fatigue liquid Qw in addition to the first solid material 36. Thereby, the water content of the first solid material 36 and the second solid material 37 discharged to the outside of the container 20 can be reduced.
 次に、現像装置14について説明する。現像装置14は、例えば、感光性樹脂版を水系洗い出し液を用いて現像するものである。
 現像装置14は、例えば、図2に示すように、現像槽40と、ブラシ42とが設けられている。ブラシ42は駆動部材43に設けられている。また、ブラシ42には、供給管44が設けられている。供給管44は供給部46に接続されている。現像装置14では、供給部46から供給管44を経て、ブラシ42から洗い出し液が感光性樹脂版50の表面50aに供給される。
Next, the developing device 14 will be described. The developing device 14 develops, for example, a photosensitive resin plate using an aqueous washing solution.
The developing device 14 is provided with, for example, a developing tank 40 and a brush 42 as shown in FIG. The brush 42 is provided on the driving member 43. The brush 42 is provided with a supply pipe 44. The supply pipe 44 is connected to a supply section 46. In the developing device 14, the washing liquid is supplied from the supply unit 46 to the surface 50 a of the photosensitive resin plate 50 from the brush 42 via the supply pipe 44.
 現像の際には、洗い出し液Qをブラシ42から感光性樹脂版50の表面50aに供給しながら、駆動部材43を図示しない駆動部により回転させて、ブラシ42により、露光後の感光性樹脂版50の表面50aが擦られる。これにより、露光後の未硬化部(図示せず)が感光性樹脂版50の表面50aから除去されて洗い出し液Q中に排出される。露光後の未硬化部(図示せず)が洗い出し液Qに排出された状態のものを現像疲労液Qwという。現像疲労液Qwには洗い出し液Qも含まれる。 At the time of development, the driving member 43 is rotated by a driving unit (not shown) while the washing liquid Q is supplied from the brush 42 to the surface 50 a of the photosensitive resin plate 50, and the exposed photosensitive resin plate is The surface 50a of the 50 is rubbed. As a result, the uncured portion (not shown) after the exposure is removed from the surface 50a of the photosensitive resin plate 50 and discharged into the washing liquid Q. A state in which the uncured portion (not shown) after the exposure is discharged into the washing liquid Q is referred to as a developing fatigue liquid Qw. The washing-out liquid Q is also included in the developing fatigue liquid Qw.
 現像槽40は配管31に接続されている。配管31から現像疲労液Qwとして送出される。
 配管28は供給管44に接続されている。配管28と供給管44との間にはバルブ47が設けられている。バルブ47の開閉により、配管28と供給管44との連通が制御される。供給管44に処理済みの現像疲労液Qwを供給しない場合には、バルブ47は閉じられている。
 配管28を経て処理済みの現像疲労液Qwが供給管44から感光性樹脂版50に供給される。この場合、バルブ47は開けられている。図9に示す別の実施形態の処理装置12では、配管28には、上述のように分離膜30が設けられており、処理済みの現像疲労液Qwは、分離膜30を通過されて供給される。
The developing tank 40 is connected to the pipe 31. It is sent out from the pipe 31 as a developing fatigue liquid Qw.
The pipe 28 is connected to a supply pipe 44. A valve 47 is provided between the pipe 28 and the supply pipe 44. The opening and closing of the valve 47 controls the communication between the pipe 28 and the supply pipe 44. When the processed developing fatigue liquid Qw is not supplied to the supply pipe 44, the valve 47 is closed.
The processed developing fatigue liquid Qw is supplied from the supply pipe 44 to the photosensitive resin plate 50 via the pipe 28. In this case, the valve 47 is open. In the processing apparatus 12 of another embodiment shown in FIG. 9, the separation film 30 is provided in the pipe 28 as described above, and the processed development fatigue solution Qw is supplied through the separation film 30. You.
 なお、現像装置14は、現像方式は特に限定されるものではなく、バッチ式でも搬送式でもよい。また、現像装置14は、洗い出し液を感光性樹脂版50に噴霧して、未露光部を除去する形態でもよく、感光性樹脂版50を洗い出し液中に浸漬して、未露光部を除去する形態でもよい。
 感光性樹脂版50は、その構成は特に限定されるものではなく、例えば、フレキソ印刷に使用されるフレキソ印刷版を形成するものである。感光性樹脂版50は、水を主成分とする水系現像液で現像可能なもの、水現像型のフレキソ印刷版原版と呼ばれるものであることが好ましい。感光性樹脂版50には、水系現像液で現像可能な公知のフレキソ印刷版原版が利用可能であり、表面にブラックレイヤー層が塗布された、CTP(Computer To Plate)対応のフレキソ版材でもよい。
The developing system of the developing device 14 is not particularly limited, and may be a batch system or a transport system. Further, the developing device 14 may be configured to spray the washing liquid onto the photosensitive resin plate 50 to remove the unexposed portions, or to immerse the photosensitive resin plate 50 in the washing solution to remove the unexposed portions. It may be in a form.
The configuration of the photosensitive resin plate 50 is not particularly limited. For example, the photosensitive resin plate 50 forms a flexographic printing plate used for flexographic printing. The photosensitive resin plate 50 is preferably one that can be developed with an aqueous developer mainly containing water, or one that is called a water-developing type flexographic printing plate precursor. As the photosensitive resin plate 50, a known flexographic printing plate precursor that can be developed with an aqueous developer can be used, and a CTP (Computer To Plate) -compatible flexographic plate material having a black layer layer coated on the surface may be used. .
 次に、処理方法について説明する。
 処理方法では、現像疲労液Qwを容器20内に供給しながら、容器20を回転し、現像疲労液Qwに含まれる固形物を遠心分離し、その後、現像疲労液Qwの供給を停止し、一定時間の間、容器20の回転を継続した後、容器20の回転を停止する。容器20を回転させて、キーパーディスク23に保持された固形物を、キーパーディスク23から取り除く。
 以下、より詳細に処理方法について説明する。図3~図5に示す模式図は、本発明の実施形態の処理装置の一例を有する処理システムを用いた処理方法を工程順に示すものである。なお、図3~図5に示すシステム10において、図1に示す処理システム10と同一構成物には同一符号を付して、その詳細な説明は省略する。また、図3および図4ではスクレーパー34の図示を省略している。
 処理方法では、まず、露光装置(図示せず)により感光性樹脂版50(図2参照)の表面50a(図2参照)を、画像様露光、すなわち、特定のパターンで露光する。
 画像様露光後の感光性樹脂版50を、現像装置14に搬送し、現像装置14において、現像槽40(図2参照)内にて、洗い出し液Q中でブラシ42(図2参照)を用いて感光性樹脂版50(図2参照)を現像する。洗い出し液Qを用いた現像によって、画像様露光後の感光性樹脂版50の未露光部が除去されることにより発生した固形物が洗い出し液Q(図2参照)中に分散する。これにより、固形物を含んだ現像疲労液Qwが発生する。
Next, a processing method will be described.
In the processing method, the container 20 is rotated while supplying the developing fatigue solution Qw into the container 20, and the solid matter contained in the developing fatigue solution Qw is centrifuged. Thereafter, the supply of the developing fatigue solution Qw is stopped, and After the rotation of the container 20 is continued during the time, the rotation of the container 20 is stopped. The container 20 is rotated to remove solid matter held by the keeper disk 23 from the keeper disk 23.
Hereinafter, the processing method will be described in more detail. The schematic diagrams shown in FIGS. 3 to 5 show a processing method using a processing system having an example of the processing apparatus according to the embodiment of the present invention in the order of steps. In the system 10 shown in FIGS. 3 to 5, the same components as those of the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted. 3 and 4, illustration of the scraper 34 is omitted.
In the processing method, first, the surface 50a (see FIG. 2) of the photosensitive resin plate 50 (see FIG. 2) is imagewise exposed, that is, exposed in a specific pattern by an exposure device (not shown).
The photosensitive resin plate 50 after the imagewise exposure is transported to the developing device 14, where the brush 42 (see FIG. 2) is used in the washing solution Q in the developing tank 40 (see FIG. 2). To develop the photosensitive resin plate 50 (see FIG. 2). By the development using the washing liquid Q, the solid matter generated by removing the unexposed portions of the photosensitive resin plate 50 after the imagewise exposure is dispersed in the washing liquid Q (see FIG. 2). As a result, a development fatigue liquid Qw containing a solid is generated.
 駆動部26により中心軸Cを回転軸として回転する容器20内に、現像装置14から配管31を介して現像疲労液Qwが供給される。
 中心軸Cを回転軸とする容器20の回転により、現像疲労液Qwに含まれる第1の固形物36と第2の固形物37とを遠心分離する。遠心分離により、容器20内で現像疲労液Qwに含まれる固形物が質量に応じて分離する。容器20内で第1の固形物36と第2の固形物37とを、予め定められた回転数および回転時間等の遠心分離条件にて遠心分離し、図3に示すように第2の固形物37を容器20の内壁20gに集積し、第1の固形物36を容器20内に設けられたキーパーディスク23に集積させる(第1の工程)。なお、上述の遠心分離の際に、容器20内の現像疲労液Qwは、大半が開口部21bから溢れ出てケース24に貯留される。ケース24に排出された現像疲労液Qwは排出路25を経て消泡タンク27に貯留される。
The developing fatigue liquid Qw is supplied from the developing device 14 to the container 20 rotated about the central axis C by the driving unit 26 via the pipe 31.
By rotating the container 20 about the central axis C as a rotation axis, the first solid matter 36 and the second solid matter 37 contained in the developing fatigue liquid Qw are centrifuged. By the centrifugation, the solid matter contained in the developing fatigue solution Qw is separated in the container 20 according to the mass. The first solid material 36 and the second solid material 37 are centrifuged in the container 20 under predetermined centrifugation conditions such as the number of rotations and the rotation time, and as shown in FIG. The objects 37 are accumulated on the inner wall 20g of the container 20, and the first solids 36 are accumulated on the keeper disk 23 provided in the container 20 (first step). At the time of the above-described centrifugal separation, most of the developing fatigue liquid Qw in the container 20 overflows from the opening 21b and is stored in the case 24. The developing fatigue solution Qw discharged to the case 24 is stored in the defoaming tank 27 via the discharging path 25.
 次に、回転する容器20への現像疲労液Qwの供給を停止し、一定時間の間、駆動部26による容器20の回転を継続する(第2の工程)。このとき、第2の工程では、第1の固形物36がキーパーディスク23に保持された状態にある。第2の工程でも、一定時間の間とは、上述のように、例えば、10分以下であり、より好ましくは30秒~5分であり、更に好ましくは1~3分である。上述の一定時間の間において、現像疲労液Qwの供給は停止されている。例えば、以下の工程でも、現像疲労液Qwの供給は停止されている。なお、一定時間経過した後、現像疲労液Qwを供給することもできる。
 次に、第1の固形物36がキーパーディスク23に保持された状態で、駆動部26による容器20の回転を停止する(第3の工程)。すなわち、遠心分離を停止する。
Next, the supply of the developing fatigue solution Qw to the rotating container 20 is stopped, and the rotation of the container 20 by the driving unit 26 is continued for a predetermined time (second step). At this time, in the second step, the first solid material 36 is held by the keeper disk 23. Also in the second step, as described above, for a certain period of time, for example, is 10 minutes or less, more preferably 30 seconds to 5 minutes, and still more preferably 1 to 3 minutes. During the above-mentioned fixed time, the supply of the developing fatigue liquid Qw is stopped. For example, also in the following steps, the supply of the developing fatigue liquid Qw is stopped. After a certain period of time, the developing fatigue liquid Qw can be supplied.
Next, the rotation of the container 20 by the drive unit 26 is stopped while the first solid material 36 is held by the keeper disk 23 (third step). That is, centrifugation is stopped.
 次に、駆動部26により、容器20を回転させて、再度遠心分離を実施する。回転の際に作用する遠心力により、キーパーディスク23に保持された第1の固形物36はキーパーディスク23上から取り除かれる(第4の工程)。このとき、図4に示すように第1の固形物36は吹き飛ばされて容器20の胴部20aの内壁20gに堆積するが、第2の固形物37も容器20の回転の際に遠心力を受けて容器20の胴部20aの内壁20gに保持されたままである。このため、第1の固形物36と第2の固形物37とが胴部20aの内壁20gに堆積される。この状態で、内壁20gの堆積物を除去することにより、第1の固形物36と第2の固形物37とが同時に容器20から除去される。
 なお、第1の固形物36と第2の固形物37とが除去されるため、除去された第1の固形物36および第2の固形物37は含水率が低い。このため、第1の固形物36と第2の固形物37とを固体廃棄物として廃棄する際、廃棄量を少なくできる。
 また、回転する容器20内に供給していた現像疲労液Qwの供給を停止し、一定時間の間、容器20の回転を継続した後、容器20の回転を停止し、容器20を回転させている。これにより、固液分離性が向上し、回収する固形物の量を多くすることができる。
Next, the container 20 is rotated by the drive unit 26, and centrifugation is performed again. The first solid material 36 held on the keeper disk 23 is removed from the keeper disk 23 by the centrifugal force acting upon rotation (fourth step). At this time, as shown in FIG. 4, the first solid 36 is blown off and deposited on the inner wall 20 g of the body 20 a of the container 20, but the second solid 37 also exerts a centrifugal force when the container 20 rotates. The container 20 is held on the inner wall 20g of the body 20a of the container 20. Therefore, the first solid matter 36 and the second solid matter 37 are deposited on the inner wall 20g of the body 20a. In this state, the first solid matter 36 and the second solid matter 37 are simultaneously removed from the container 20 by removing the deposit on the inner wall 20g.
Since the first solids 36 and the second solids 37 are removed, the removed first solids 36 and the second solids 37 have a low moisture content. Therefore, when the first solid material 36 and the second solid material 37 are discarded as solid waste, the amount of waste can be reduced.
Further, the supply of the developing fatigue solution Qw supplied to the rotating container 20 is stopped, and after the container 20 is continuously rotated for a certain period of time, the rotation of the container 20 is stopped and the container 20 is rotated. I have. Thereby, the solid-liquid separation property is improved, and the amount of the collected solid can be increased.
 消泡タンク27に貯留された現像疲労液Qwを、ポンプ29により、配管28を介して現像装置14に返送する。このとき、図9に示す第2の例の実施形態の処理装置12では、配管28に分離膜30が設けられているため、現像疲労液Qwに含まれる固形物が取り除かれて、現像装置14に現像疲労液Qwが返送される。現像疲労液Qwが洗い出し液Q(図2参照)、あるいは未露光部を現像除去した後に、感光性樹脂版50の版面に残存するカスを洗い流すリンス液として使用される。 (4) The developing fatigue solution Qw stored in the defoaming tank 27 is returned to the developing device 14 via the pipe 28 by the pump 29. At this time, in the processing apparatus 12 of the second embodiment shown in FIG. 9, since the separation film 30 is provided in the pipe 28, the solid matter contained in the developing fatigue liquid Qw is removed, and the developing apparatus 14 Is returned to the developing fatigue solution Qw. The development fatigue solution Qw is used as a washing solution Q (see FIG. 2) or a rinsing solution for washing off the residue remaining on the plate surface of the photosensitive resin plate 50 after developing and removing the unexposed portion.
 容器20内に存在する第1の固形物36と第2の固形物37は、除去部33で除去されるが、図5を用いて説明する。
 除去部33を用いて容器20内の固形物を除去する場合、図5に示すように、傾斜部20bの開口部20fにシャッター21cを開け、かつ底部20cの底面20dを開けた状態で、底面20dの下方に受皿32を配置する。この状態で、図6に示すようにスクレーパー34を、容器20が回転する方向Rと反対の方向rに回転させる。これにより、容器20の内壁20gに堆積した第1の固形物36と第2の固形物37とが掻き取られ、内壁20gに堆積した第1の固形物36と第2の固形物37とが同時に容器20内から除去される。
The first solid matter 36 and the second solid matter 37 present in the container 20 are removed by the removing unit 33, which will be described with reference to FIG.
When removing the solid matter in the container 20 using the removing unit 33, as shown in FIG. 5, the shutter 21c is opened at the opening 20f of the inclined portion 20b, and the bottom surface 20d of the bottom portion 20c is opened. The pan 32 is arranged below 20d. In this state, the scraper 34 is rotated in the direction r opposite to the direction R in which the container 20 rotates, as shown in FIG. Thereby, the first solid matter 36 and the second solid matter 37 deposited on the inner wall 20g of the container 20 are scraped off, and the first solid matter 36 and the second solid matter 37 deposited on the inner wall 20g are separated. At the same time, it is removed from the container 20.
 なお、上述の処理方法では第1の固形物36と第2の固形物37とを同時に除去したが、これに限定されるものではなく、別々に除去してもよい。例えば、遠心分離を停止した後、すなわち、第3の工程と第4の工程との間で、スクレーパー34(図1参照)により、容器20の内壁20gに堆積した第2の固形物37を容器20から除去する。その後、再度容器20を回転させて(第4の工程)、第1の固形物36をキーパーディスク23上から取り除き、第1の固形物36を容器20の内壁20gに堆積させる。その後、スクレーパー34(図1参照)により第1の固形物36を容器20から除去する。
 上述のように第1の固形物36と第2の固形物37とを別々に除去する場合でも、容器20から現像疲労液Qwが排出された状態で除去されるため、第1の固形物36と第2の固形物37とは含水率が低い状態で除去される。このため、第1の固形物36と第2の固形物37とを固体廃棄物として廃棄する際、廃棄量を少なくできる。
 なお、容器20内から除去された第1の固形物36と第2の固形物37には、その後、脱水工程を設けて、更に含水率を低下させて、固体廃棄物として廃棄する際の廃棄量を削減することができる。その場合の脱水工程としては、真空式、加熱式、加圧式および遠心式等を用いることができるが、これらに限定されるものではない。
In the above-described processing method, the first solid matter 36 and the second solid matter 37 are removed at the same time, but the present invention is not limited to this, and they may be removed separately. For example, after the centrifugation is stopped, that is, between the third step and the fourth step, the second solid substance 37 deposited on the inner wall 20g of the container 20 is removed by the scraper 34 (see FIG. 1). Remove from 20. Thereafter, the container 20 is rotated again (fourth step), the first solid material 36 is removed from the keeper disk 23, and the first solid material 36 is deposited on the inner wall 20 g of the container 20. Thereafter, the first solid matter 36 is removed from the container 20 by a scraper 34 (see FIG. 1).
Even when the first solid matter 36 and the second solid matter 37 are separately removed as described above, since the developing fatigue liquid Qw is removed from the container 20 in a discharged state, the first solid matter 36 is removed. And the second solid substance 37 are removed in a state where the water content is low. Therefore, when the first solid material 36 and the second solid material 37 are discarded as solid waste, the amount of waste can be reduced.
The first solid matter 36 and the second solid matter 37 removed from the container 20 are then provided with a dehydration step to further reduce the water content and to be disposed of when discarded as solid waste. The amount can be reduced. As a dehydration step in this case, a vacuum type, a heating type, a pressure type, a centrifugal type, or the like can be used, but it is not limited thereto.
 処理装置12では図6に示すようにスクレーパー34を1つ設ける構成としたが、これに限定されるものではなく、例えば、図7に示すように、2つスクレーパー34を有する構成でもよい。この場合、除去効率の観点から、スクレーパー34を対角に配置することが好ましい。さらには、図示はしないが、スクレーパー34を4つ設ける構成でもよい。この場合、スクレーパー34は、中心軸Cに対して等間隔、すなわち、90°間隔で配置することが除去効率の観点から好ましい。なお、スクレーパー34は、内壁20gに沿って移動する平板に限定されるものではない。 (6) Although the processing apparatus 12 has a configuration in which one scraper 34 is provided as shown in FIG. 6, the present invention is not limited to this. For example, a configuration having two scrapers 34 as shown in FIG. In this case, it is preferable to dispose the scrapers 34 diagonally from the viewpoint of removal efficiency. Further, although not shown, a configuration in which four scrapers 34 are provided may be employed. In this case, it is preferable from the viewpoint of removal efficiency that the scrapers 34 be arranged at regular intervals with respect to the central axis C, that is, at 90 ° intervals. Note that the scraper 34 is not limited to a flat plate that moves along the inner wall 20g.
 また、除去部33の構成としては、スクレーパー34を容器20内に配置したが、これに限定されるものではなく、除去するときに、容器20内にスクレーパー34を挿入するようにしてもよい。除去するときに、容器20内にスクレーパー34を挿入する除去部33を処理装置12とは別体に設けてもよい。
 また、スクレーパー34の他に、圧縮エアーを容器20の内壁20gに噴出する手段(図示せず)を設け、スクレーパー34の固形物除去動作と同時あるいはその前後に圧縮エアーを噴出させてもよい。
Further, as the configuration of the removing unit 33, the scraper 34 is disposed in the container 20, but the present invention is not limited to this. The scraper 34 may be inserted into the container 20 when removing. When removing, the removing unit 33 for inserting the scraper 34 into the container 20 may be provided separately from the processing apparatus 12.
Further, in addition to the scraper 34, a means (not shown) for injecting compressed air to the inner wall 20g of the container 20 may be provided, and the compressed air may be ejected simultaneously with or before and after the solid material removing operation of the scraper 34.
 上述の処理装置12では、いずれもキーパーディスク23を3つ設ける構成としたが、これに限定されるものではなく、図8に示すようにキーパーディスク60を少なくとも1つ設ける構成であればよい。キーパーディスク60は、例えば、開口60aと本体部60bで構成された円板である。キーパーディスク60の本体部60bは遠心分離により上述の第1の固形物36が集積される位置にあればよい。なお、図8は容器20だけを示す。
 図8ではキーパーディスク60としたが、キーパーディスク60に代えて、図1に示す開口のない円板のキーパーディスク23でもよい。
In the processing device 12 described above, all three keeper disks 23 are provided. However, the configuration is not limited to this, and any configuration may be used as long as at least one keeper disk 60 is provided as shown in FIG. The keeper disk 60 is, for example, a disk having an opening 60a and a main body 60b. The main body 60b of the keeper disk 60 may be located at a position where the first solids 36 are accumulated by centrifugation. FIG. 8 shows only the container 20.
In FIG. 8, the keeper disk 60 is used, but the keeper disk 60 may be replaced with the disk-shaped keeper disk 23 having no opening shown in FIG.
 また、上述の現像疲労液Qwの処理方法において、容器20から排出された現像疲労液Qwを洗い出し液として再使用する工程、または容器20から排出された現像疲労液Qwを、現像により発生する固形物を除去する分離膜30(図9参照)を通過させて洗い出し液として再使用する工程を有してもよい。上述のように、現像疲労液Qwは分離膜30を通過させた方が、現像疲労液Qwを繰り返し使用することができるため好ましい。 Further, in the processing method of the developing fatigue liquid Qw described above, a step of reusing the developing fatigue liquid Qw discharged from the container 20 as a washing liquid, or the developing fatigue liquid Qw discharged from the container 20 may be used as a solid generated by development. There may be provided a step of passing through a separation membrane 30 (see FIG. 9) for removing substances and reusing it as a washing solution. As described above, it is preferable that the development fatigue liquid Qw be passed through the separation membrane 30 because the development fatigue liquid Qw can be used repeatedly.
 処理装置としては、上述の構成に限定されるものではなく、他の構成でもよく、以下、処理装置の他の構成について説明する。
 図10は本発明の実施形態の処理装置の第3の例を有する処理システムを示す模式図である。なお、図10に示す処理システム10bにおいて、図1に示す処理システム10と同一構成物には同一符号を付して、その詳細な説明は省略する。
 図10に示す処理システム10bは、図1に示す処理システム10に比して、容器20から排出された現像疲労液Qwを貯留し、かつ排出された現像疲労液Qwの一部を容器20に戻す供給部74を備える貯留槽70を有する点、および貯留槽70から溢れた現像疲労液Qwが配管75を介して消泡タンク27に供給される点が異なり、それ以外の構成は、図1に示す処理システム10と同じである。
The processing device is not limited to the above-described configuration, and may have another configuration. Hereinafter, another configuration of the processing device will be described.
FIG. 10 is a schematic diagram showing a processing system having a third example of the processing apparatus according to the embodiment of the present invention. In the processing system 10b shown in FIG. 10, the same components as those in the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
The processing system 10b shown in FIG. 10 stores the developing fatigue liquid Qw discharged from the container 20 and a part of the discharged developing fatigue liquid Qw in the container 20 as compared with the processing system 10 shown in FIG. The difference is that a storage tank 70 having a return supply unit 74 is provided, and that the developing fatigue solution Qw overflowing from the storage tank 70 is supplied to the defoaming tank 27 via a pipe 75. Is the same as the processing system 10 shown in FIG.
 貯留槽70は、ケース24内の下部に設けられている。貯留槽70は現像疲労液Qwを貯留することができれば、その構成は特に限定されるものではない。例えば、容器20の傾斜部20bに、管状の排出路21dが設けられており、排出路21dから貯留槽70に現像疲労液Qwが排出される。貯留槽70に現像疲労液Qwを排出することができれば、排出路21dに限定されるものではない。容器20内の現像疲労液Qwは回転時には、容器20の開口部21bから溢れ出るが、停止した状態では排出路21dを経て貯留槽70に排出される。容器20内においてキーパーディスク23が設けられていないシャッター21c側の領域には、現像疲労液Qwの固形物を保持するものがない。このため、排出路21dから貯留槽70に排出される現像疲労液Qwは固形物の含有量が多いが、貯留槽70の現像疲労液Qwが再度、遠心分離処理されるため、固形物の回収量をより多くすることができ、固液分離性が向上する。 The storage tank 70 is provided at a lower part in the case 24. The configuration of the storage tank 70 is not particularly limited as long as it can store the developing fatigue solution Qw. For example, a tubular discharge path 21d is provided in the inclined portion 20b of the container 20, and the developing fatigue liquid Qw is discharged from the discharge path 21d to the storage tank 70. The discharge path is not limited to the discharge path 21d as long as the developer fatigue liquid Qw can be discharged into the storage tank 70. The developing fatigue liquid Qw in the container 20 overflows from the opening 21b of the container 20 during rotation, but is discharged to the storage tank 70 via the discharge path 21d when stopped. In the region on the shutter 21c side where the keeper disk 23 is not provided in the container 20, there is nothing holding the solid matter of the developing fatigue liquid Qw. Therefore, although the developing fatigue liquid Qw discharged from the discharge passage 21d to the storage tank 70 has a large solid content, the developing fatigue liquid Qw in the storage tank 70 is subjected to the centrifugal separation process again, so that the solid substance is recovered. The amount can be increased, and the solid-liquid separation property is improved.
 貯留槽70には配管71が設けられており、配管71はポンプ72に接続されている。ポンプ72には、貯留槽70内の現像疲労液Qwの一部を容器20内に戻す配管73が配置されている。配管73は、配管31と同様に、例えば、配管73の開口73aが、インサイドディスク22と、一番上のキーパーディスク23との間に配置されている。配管73の開口73aはインサイドディスク22の下側であれば、その位置は特に限定されるものではない。
 ポンプ72は、制御部38に接続されている。制御部38によりポンプ72の動作が制御され、ポンプ72により貯留槽70内の現像疲労液Qwの一部が配管71および配管73を経て容器20内に戻される。
A pipe 71 is provided in the storage tank 70, and the pipe 71 is connected to a pump 72. The pump 72 is provided with a pipe 73 for returning a part of the development fatigue solution Qw in the storage tank 70 to the inside of the container 20. In the pipe 73, similarly to the pipe 31, for example, an opening 73 a of the pipe 73 is arranged between the inside disk 22 and the uppermost keeper disk 23. The position of the opening 73a of the pipe 73 is not particularly limited as long as it is below the inside disk 22.
The pump 72 is connected to the control unit 38. The operation of the pump 72 is controlled by the control unit 38, and a part of the developing fatigue solution Qw in the storage tank 70 is returned to the container 20 via the pipe 71 and the pipe 73 by the pump 72.
 図10に示す処理システム10bでは、上述のように図1に示す処理システム10と同じ処理方法により、現像疲労液Qwについて、洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを除去することができる。
 さらに、図10に示す処理システム10bでは、貯留槽70内の現像疲労液Qwがある状態、例えば、遠心分離処理を少なくとも1度、実施した後、容器20から排出された現像疲労液Qwの一部を容器20に戻し、容器20を回転させて容器20内の現像疲労液Qwを遠心分離し、第1の固形物36(図3参照)をキーパーディスク23に集積させた後、容器20内の現像疲労液Qwを、排出路21dを経て容器20内から排出する。次に、キーパーディスク23に集積された第1の固形物36(図3参照)がキーパーディスク23に保持された状態で、容器20の回転を停止した後、再度、容器20を回転させる。これにより、第1の固形物36をキーパーディスク23上から取り除き、第1の固形物36を容器20の内壁20gに堆積させる。その後、スクレーパー34(図1参照)により第1の固形物36(図3参照)を容器20から除去する。このようにして、貯留槽70内の現像疲労液Qwがある状態、例えば、遠心分離処理を少なくとも1度、実施した後、容器20から排出された現像疲労液Qwを含め、容器20内に残っている現像疲労液Qw等と一緒に遠心分離処理を実施する。これにより、図10に示す処理システム10bでは、洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを除去することができる。
In the processing system 10b shown in FIG. 10, as described above, by the same processing method as the processing system 10 shown in FIG. The second solid having a large specific gravity can be removed.
Further, in the processing system 10b shown in FIG. 10, in a state where the developing fatigue liquid Qw in the storage tank 70 is present, for example, the centrifugal separation process is performed at least once, and then the developing fatigue liquid Qw discharged from the container 20 is removed. The portion is returned to the container 20, and the container 20 is rotated to centrifuge the developing fatigue liquid Qw in the container 20, and the first solid matter 36 (see FIG. 3) is accumulated on the keeper disk 23. Is discharged from the container 20 through the discharge path 21d. Next, while the rotation of the container 20 is stopped in a state where the first solids 36 (see FIG. 3) accumulated on the keeper disk 23 are held by the keeper disk 23, the container 20 is rotated again. As a result, the first solids 36 are removed from the keeper disk 23, and the first solids 36 are deposited on the inner wall 20 g of the container 20. Thereafter, the first solid matter 36 (see FIG. 3) is removed from the container 20 by the scraper 34 (see FIG. 1). In this way, the developing fatigue solution Qw in the storage tank 70 remains in the container 20 including the developing fatigue solution Qw discharged from the container 20 after the centrifugal separation process is performed at least once, for example. A centrifugal separation process is performed together with the developing fatigue solution Qw and the like. Thereby, in the processing system 10b shown in FIG. 10, the first solid having a lower specific gravity than the rinsing liquid and the second solid having a higher specific gravity than the rinsing liquid can be removed.
 図11は本発明の実施形態の処理装置の第4の例を有する処理システムを示す模式図である。なお、図11に示す処理システム10cにおいて、図10に示す処理システム10cと同一構成物には同一符号を付して、その詳細な説明は省略する。
 図11に示す処理システム10cは、図10に示す処理システム10bに比して、現像装置14の配管31が容器20内に現像疲労液Qwを供給するものではなく、消泡タンク27に接続されている点、および消泡タンク27内の現像疲労液Qwを容器20内に送液する送液部84を有する点が異なり、それ以外の構成は、図10に示す処理システム10bと同じである。
FIG. 11 is a schematic diagram showing a processing system having a fourth example of the processing apparatus according to the embodiment of the present invention. In the processing system 10c illustrated in FIG. 11, the same components as those of the processing system 10c illustrated in FIG. 10 are denoted by the same reference numerals, and detailed description thereof will be omitted.
The processing system 10c shown in FIG. 11 is different from the processing system 10b shown in FIG. 10 in that the pipe 31 of the developing device 14 does not supply the developing fatigue liquid Qw into the container 20 but is connected to the defoaming tank 27. And a liquid sending section 84 for sending the developing fatigue liquid Qw in the defoaming tank 27 into the container 20. The other configuration is the same as the processing system 10b shown in FIG. .
 送液部84は、消泡タンク27に設けられた配管81と、配管81に接続されたポンプ82と、ポンプ82に接続された配管83とを有する。
 配管83については、図1に示す処理システム10の配管31と同様に、例えば、配管83の開口83aが、インサイドディスク22と、一番上のキーパーディスク23との間に配置されている。配管83の開口83aはインサイドディスク22の下側であれば、その位置は特に限定されるものではない。
 ポンプ82は、制御部38に接続されている。制御部38によりポンプ82の動作が制御され、ポンプ82により消泡タンク27内の現像疲労液Qwが配管81および配管83を経て容器20内に送液される。
The liquid sending section 84 has a pipe 81 provided in the defoaming tank 27, a pump 82 connected to the pipe 81, and a pipe 83 connected to the pump 82.
As for the pipe 83, for example, the opening 83 a of the pipe 83 is disposed between the inside disk 22 and the uppermost keeper disk 23, similarly to the pipe 31 of the processing system 10 shown in FIG. 1. The position of the opening 83a of the pipe 83 is not particularly limited as long as it is below the inside disk 22.
The pump 82 is connected to the control unit 38. The operation of the pump 82 is controlled by the control unit 38, and the developing fatigue liquid Qw in the defoaming tank 27 is sent into the container 20 via the pipes 81 and 83 by the pump 82.
 図11に示す処理システム10cでは、現像疲労液Qwが、現像装置14から処理装置12に直接供給されるのではなく、消泡タンク27に貯留された後に、送液部84により容器20内に送液される。処理システム10cでは、消泡タンク27、現像装置14および消泡タンク27の系統と、消泡タンク27、処理装置12および消泡タンク27の系統が存在し、各系統をそれぞれ互いに独立に動作させることができる。このため、現像装置14の動作サイクルの影響を受けることなく、処理装置12を動作させて、現像疲労液Qwから固形分を除去することができる。処理システム10cは、図1に示す処理システム10および図10に示す処理システム10bに比して、処理装置12の動作の自由度が高い。
 なお、図10の処理システム10bおよび図11に示す処理システム10cは、いずれも図9に示す分離膜30を有する構成でもよい。
In the processing system 10c shown in FIG. 11, the developing fatigue solution Qw is not directly supplied from the developing device 14 to the processing device 12, but is stored in the defoaming tank 27, and is then stored in the container 20 by the liquid sending section 84. It is sent. In the processing system 10c, there are a system of the defoaming tank 27, the developing device 14, and the defoaming tank 27, and a system of the defoaming tank 27, the processing device 12, and the defoaming tank 27, and these systems are operated independently of each other. be able to. Therefore, the processing device 12 can be operated to remove solid components from the developing fatigue liquid Qw without being affected by the operation cycle of the developing device 14. The processing system 10c has a higher degree of freedom in the operation of the processing device 12 than the processing system 10 illustrated in FIG. 1 and the processing system 10b illustrated in FIG.
Note that each of the processing system 10b in FIG. 10 and the processing system 10c in FIG. 11 may have a configuration having the separation membrane 30 shown in FIG.
 図11に示す処理システム10cでは、上述のように図1に示す処理システム10と同じ処理方法により、現像疲労液Qwについて、洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを除去することができる。
 また、図11に示す処理システム10cでは、上述の図10に示す処理システム10bと同じ処理方法を行うこともでき、遠心分離処理を少なくとも1度、実施した後、容器20から排出された現像疲労液Qwを含め、図10に示す処理システム10bでは、洗い出し液よりも比重の小さい第1の固形物と、洗い出し液よりも比重の大きい第2の固形物とを除去することができる。
In the processing system 10c shown in FIG. 11, as described above, by the same processing method as the processing system 10 shown in FIG. The second solid having a large specific gravity can be removed.
Further, in the processing system 10c illustrated in FIG. 11, the same processing method as the processing system 10b illustrated in FIG. 10 described above can be performed, and the centrifugal separation process is performed at least once, and then the development fatigue discharged from the container 20 is reduced. In the processing system 10b shown in FIG. 10, including the liquid Qw, the first solid having a lower specific gravity than the washing liquid and the second solid having a higher specific gravity than the washing liquid can be removed.
 図12は、比較のための処理装置を有する処理システムを示す模式図である。
 なお、図12に示す処理システム100において、図1に示す処理システム10と同一構成物には同一符号を付して、その詳細な説明は省略する。
 図12に示す処理システム100は、図1に示す処理システム10に比して、処理装置102にキーパーディスク23(図1参照)が設けられていない点が異なり、それ以外の構成は図1に示す処理システム10と同じである。
FIG. 12 is a schematic diagram showing a processing system having a processing device for comparison.
In the processing system 100 shown in FIG. 12, the same components as those of the processing system 10 shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.
The processing system 100 shown in FIG. 12 is different from the processing system 10 shown in FIG. 1 in that the processing device 102 is not provided with the keeper disk 23 (see FIG. 1). It is the same as the processing system 10 shown.
 図12に示すように、キーパーディスク23が設けられていない処理装置102では、容器20を回転させて遠心分離する際、遠心力により、第1の固形物36は質量に応じた位置に集積する。しかしながら、容器20の回転を停止すると、第1の固形物36が傾斜部20bの内面104に堆積する。この状態で、上述の処理方法のように、容器20内の現像疲労液Qwをケース24に排出すると、ケース24内に排出される現像疲労液Qwは第1の固形物36を多く含み、現像疲労液Qwの固形分濃度が上がる懸念がある。
 また、傾斜部20bの内面104の堆積量が多いと、除去する際に手間がかかる。
As shown in FIG. 12, in the processing apparatus 102 in which the keeper disk 23 is not provided, when the container 20 is rotated and centrifuged, the first solids 36 accumulate at a position corresponding to the mass due to the centrifugal force. . However, when the rotation of the container 20 is stopped, the first solids 36 accumulate on the inner surface 104 of the inclined portion 20b. In this state, when the developing fatigue solution Qw in the container 20 is discharged into the case 24 as in the processing method described above, the developing fatigue solution Qw discharged into the case 24 contains a large amount of the first solid matter 36, There is a concern that the solid content concentration of the fatigue fluid Qw will increase.
In addition, when the amount of deposition on the inner surface 104 of the inclined portion 20b is large, it takes time to remove it.
 以下、現像疲労液について詳細に説明する。
 <現像疲労液>
 本発明の処理方法の処理対象である現像疲労液は、洗い出し液を用いた現像によって未露光部が除去されることより発生する固形物を含む洗い出し液、すなわち、未硬化樹脂を含む洗い出し液であれば特に限定されるものではない。しかしながら、一般的な感光性樹脂層を形成するための従来公知の感光性樹脂組成物を含む現像疲労液を処理対象とすることができる。
 また、処理方法は、LAM(Laser Ablation Masking)方式で現像した際の現像疲労液を処理対象とすることが好ましいため、現像により除去される未硬化樹脂は、感光性樹脂組成物に含まれる感光性樹脂であることが好ましい。
 また、このような感光性樹脂組成物としては、感光性樹脂の他に、例えば、重合開始剤、重合性化合物、重合禁止剤、および可塑剤等を含有する組成物が挙げられるため、本発明の処理方法の処理対象である現像疲労液は、未硬化樹脂の他に、重合開始剤、重合性化合物、重合禁止剤、および可塑剤等を含有していてもよい。
Hereinafter, the developing fatigue liquid will be described in detail.
<Development fatigue fluid>
The development fatigue solution to be processed by the processing method of the present invention is a washing solution containing solid matter generated by removing unexposed portions by development using a washing solution, that is, a washing solution containing an uncured resin. If there is, it is not particularly limited. However, a developing fatigue solution containing a conventionally known photosensitive resin composition for forming a general photosensitive resin layer can be treated.
In addition, since the processing method is preferably a processing fatigue developing solution when developed by a laser ablation masking (LAM) method, the uncured resin removed by the development is a photosensitive resin contained in the photosensitive resin composition. It is preferably a conductive resin.
In addition, such a photosensitive resin composition includes, in addition to the photosensitive resin, for example, a composition containing a polymerization initiator, a polymerizable compound, a polymerization inhibitor, a plasticizer, and the like. The developing fatigue liquid to be processed by the processing method of (1) may contain a polymerization initiator, a polymerizable compound, a polymerization inhibitor, a plasticizer, and the like in addition to the uncured resin.
 <未硬化樹脂>
 現像疲労液に含まれる未硬化樹脂とは、未露光部が除去されることにより発生する固形物のことである。現像疲労液に含まれる未硬化樹脂としては、例えば、水分散性ラテックス、ゴム成分、ポリマー成分、および未架橋のエチレン性不飽和化合物(重合体)等が挙げられる。
 水分散性ラテックスとしては、ポリブタジエンラテックス、天然ゴムラテックス、スチレン-ブタジエン共重合体ラテックス、アクリロニトリル-ブタジエン共重合体ラテックス、ポリクロロプレンラテックス、ポリイソプレンラテックス、ポリウレタンラテックス、メチルメタクリレート-ブタジエン共重合体ラテックス、ビニルピリジン共重合体ラテックス、ブチル重合体ラテックス、チオコール重合体ラテックス、アクリレート重合体ラテックス等の水分散ラテックス等の水分散ラテックス重合体、またはこれら重合体にアクリル酸もしくはメタクリル酸等の他の成分を共重合して得られる重合体等が挙げられる。
 ゴム成分としては、ブタジエンゴム、イソプレンゴム、スチレン-ブタジエンゴム、アクリロニトリルゴム、アクリロニトリルブタジエンゴム、クロロプレンゴム、ポリウレタンゴム、シリコンゴム、ブチルゴム、エチレン-プロピレンゴム、エピクロヒドリンゴム等が挙げられる。
 ポリマー成分としては、親水性であっても、疎水性であってもよく、具体的には、ポリアミド樹脂、不飽和ポリエステル樹脂、アクリル樹脂、ポリウレタン樹脂、ポリエステル樹脂、ポリビニルアルコール樹脂等が挙げられる。
 洗い出し液よりも比重の小さい固形物は、例えば、ゴム成分およびラテックス等の感光性樹脂である。
 洗い出し液よりも比重の大きい固形物は、例えば、カーボン等のオーバーコート層の成分である。
<Uncured resin>
The uncured resin contained in the developing fatigue liquid is a solid generated by removing an unexposed portion. Examples of the uncured resin contained in the developing fatigue liquid include a water-dispersible latex, a rubber component, a polymer component, and an uncrosslinked ethylenically unsaturated compound (polymer).
Examples of the water-dispersible latex include polybutadiene latex, natural rubber latex, styrene-butadiene copolymer latex, acrylonitrile-butadiene copolymer latex, polychloroprene latex, polyisoprene latex, polyurethane latex, methyl methacrylate-butadiene copolymer latex, A water-dispersed latex polymer such as a water-dispersed latex such as vinylpyridine copolymer latex, butyl polymer latex, thiochol polymer latex, and acrylate polymer latex, or other components such as acrylic acid or methacrylic acid are added to these polymers. Examples include a polymer obtained by copolymerization.
Examples of the rubber component include butadiene rubber, isoprene rubber, styrene-butadiene rubber, acrylonitrile rubber, acrylonitrile butadiene rubber, chloroprene rubber, polyurethane rubber, silicone rubber, butyl rubber, ethylene-propylene rubber, and epichlorohydrin rubber.
The polymer component may be hydrophilic or hydrophobic, and specific examples include a polyamide resin, an unsaturated polyester resin, an acrylic resin, a polyurethane resin, a polyester resin, and a polyvinyl alcohol resin.
The solid having a lower specific gravity than the washing liquid is, for example, a photosensitive resin such as a rubber component and latex.
The solid matter having a higher specific gravity than the washing liquid is, for example, a component of the overcoat layer such as carbon.
 エチレン性不飽和化合物(重合体)としては、例えば、エチレン性不飽和結合を分子中に有する(メタ)アクリル変性重合体等を挙げることができる。
 (メタ)アクリル変性重合体としては、例えば、(メタ)アクリル変性ブタジエンゴム、(メタ)アクリル変性ニトリルゴム等を挙げることができる。
 「(メタ)アクリル」とは、アクリルまたはメタクリルを表す表記であり、後述する「(メタ)アクリレート」とは、アクリレートまたはメタクリレートを表す表記である。
Examples of the ethylenically unsaturated compound (polymer) include a (meth) acryl-modified polymer having an ethylenically unsaturated bond in a molecule.
Examples of the (meth) acryl-modified polymer include (meth) acryl-modified butadiene rubber and (meth) acryl-modified nitrile rubber.
“(Meth) acryl” is a notation representing acryl or methacryl, and “(meth) acrylate” described later is a notation representing acrylate or methacrylate.
 現像疲労液に含まれる未硬化樹脂は特に限定されないが、70質量%以下であることが好ましく、35質量%以下であることがより好ましい。 未 The uncured resin contained in the developing fatigue liquid is not particularly limited, but is preferably 70% by mass or less, more preferably 35% by mass or less.
 <重合開始剤>
 現像疲労液に含んでいてもよい重合開始剤としては、光重合開始剤であることが好ましい。
 上述の光重合開始剤としては、例えば、アルキルフェノン類、アセトフェノン類、ベンゾインエーテル類、ベンゾフェノン類、チオキサントン類、アントラキノン類、ベンジル類、およびビアセチル類等が挙げられ、なかでも、アルキルフェノン類が好ましい。
 アルキルフェノン類の光重合開始剤としては、具体的には、例えば、2,2-ジメトキシ-1,2-ジフェニルエタン-1-オン、1-ヒドロキシ-シクロヘキシル-フェニル-ケトン、および2-ヒドロキシ-2-メチル-1-フェニル-プロパン-1-オン等が挙げられる。
<Polymerization initiator>
The polymerization initiator that may be contained in the developing fatigue solution is preferably a photopolymerization initiator.
Examples of the photopolymerization initiator include, for example, alkylphenones, acetophenones, benzoin ethers, benzophenones, thioxanthones, anthraquinones, benzyls, and biacetyls, among which alkylphenones are preferable. .
Specific examples of the alkylphenone photopolymerization initiator include, for example, 2,2-dimethoxy-1,2-diphenylethan-1-one, 1-hydroxy-cyclohexyl-phenyl-ketone, and 2-hydroxy- 2-methyl-1-phenyl-propan-1-one and the like.
 現像疲労液に含んでいてもよい重合開始剤の濃度は特に限定されないが、2.0質量%以下であることが好ましく、1.0質量%以下であることがより好ましい。 濃度 The concentration of the polymerization initiator that may be contained in the developing fatigue solution is not particularly limited, but is preferably 2.0% by mass or less, more preferably 1.0% by mass or less.
 <重合性化合物>
 現像疲労液に含んでいてもよい重合性化合物としては、例えば、上述したエチレン性不飽和化合物(重合体)以外のいわゆるモノマー成分に該当するエチレン性不飽和化合物等が挙げられる。
<Polymerizable compound>
Examples of the polymerizable compound that may be contained in the developing fatigue liquid include an ethylenically unsaturated compound corresponding to a so-called monomer component other than the above-mentioned ethylenically unsaturated compound (polymer).
 エチレン性不飽和化合物は、エチレン性不飽和結合を1つ有する化合物であってもよいし、エチレン性不飽和結合を2つ以上有する化合物であってもよい。 The ethylenically unsaturated compound may be a compound having one ethylenically unsaturated bond or a compound having two or more ethylenically unsaturated bonds.
 エチレン性不飽和結合を1つ有する化合物としては、具体的には、2-ヒドロキシエチル(メタ)アクリレート、2-ヒドロキシプロピル(メタ)アクリレート、2-ヒドロキシブチル(メタ)アクリレート、3-クロロ-2-ヒドロキシプロピル(メタ)アクリレート、β-ヒドロキシ-β’-(メタ)アクリロイルオキシエチルフタレート等の水酸基を有する(メタ)アクリレート;メチル(メタ)アクリレート、エチル(メタ)アクリレート、プロピル(メタ)アクリレート、ブチル(メタ)アクリレート、イソアミル(メタ)アクリレート、2-エチルヘキシル(メタ)アクリレート、ラウリル(メタ)アクリレート、ステアリル(メタ)アクリレート等のアルキル(メタ)アクリレート;シクロヘキシル(メタ)アクリレート等のシクロアルキル(メタ)アクリレート;クロロエチル(メタ)アクリレート、クロロプロピル(メタ)アクリレート等のハロゲン化アルキル(メタ)アクリレート;メトキシエチル(メタ)アクリレート、エトキシエチル(メタ)アクリレート、ブトキシエチル(メタ)アクリレート等のアルコキシアルキル(メタ)アクリレート;フェノキシエチルアクリレート、ノニルフェノキシエチル(メタ)アクリレート等のフェノキシアルキル(メタ)アクリレート;エトキシジエチレングリコール(メタ)アクリレート、メトキシトリエチレングリコール(メタ)アクリレート、メトキシジプロピレングレコール(メタ)アクリレート等のアルコキシアルキレングリコール(メタ)アクリレート;2、2-ジメチルアミノエチル(メタ)アクリレート、2,2-ジエチルアミノエチル(メタ)アクリレート、2-ヒドロキシエチル(メタ)アクリレート、3-クロロ-2-ヒドロキシプロピル(メタ)アクリレート等を挙げることができる。 Specific examples of the compound having one ethylenically unsaturated bond include 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, 2-hydroxybutyl (meth) acrylate, and 3-chloro-2. (Hydroxy) (meth) acrylate, (meth) acrylate having a hydroxyl group such as β-hydroxy-β ′-(meth) acryloyloxyethyl phthalate; methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, Alkyl (meth) acrylates such as butyl (meth) acrylate, isoamyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, lauryl (meth) acrylate, and stearyl (meth) acrylate; cyclohexyl (meth) acrylate and the like Cycloalkyl (meth) acrylate; halogenated alkyl (meth) acrylate such as chloroethyl (meth) acrylate, chloropropyl (meth) acrylate; methoxyethyl (meth) acrylate, ethoxyethyl (meth) acrylate, butoxyethyl (meth) acrylate, and the like Alkoxyalkyl (meth) acrylates; phenoxyalkyl (meth) acrylates such as phenoxyethyl acrylate and nonylphenoxyethyl (meth) acrylate; ethoxydiethylene glycol (meth) acrylate, methoxytriethylene glycol (meth) acrylate, methoxydipropylene glycol ( Alkoxyalkylene glycol (meth) acrylates such as meth) acrylate; 2,2-dimethylaminoethyl (meth) acryle DOO, 2,2-diethylaminoethyl (meth) acrylate, 2-hydroxyethyl (meth) acrylate, and 3-chloro-2-hydroxypropyl (meth) acrylate.
 エチレン性不飽和結合を2つ以上有するエチレン性不飽和化合物としては、具体的には、1,9-ノナンジオールジ(メタ)アクリレート等のアルキルジオールジ(メタ)アクリレート;ジエチレングリコールジ(メタ)アクリレート等のポリエチレングリコールジ(メタ)アクリレート;ジプロピレングリコールジ(メタ)アクリレート等のポリプロピレングリコールジ(メタ)アクリレート;トリメチロールプロパントリ(メタ)アクリレート、ペンタエリスリトールトリ(メタ)アクリレート、ペンタエリスリトールテトラ(メタ)アクリレート、グリセロールトリ(メタ)アクリレート、エチレングリコールジグリシジルエーテルに不飽和カルボン酸または不飽和アルコール等のエチレン性不飽和結合と活性水素を持つ化合物を付加反応させて得られる多価(メタ)アクリレート;グリシジル(メタ)アクリレート等の不飽和エポキシ化合物とカルボン酸またはアミンのような活性水素を有する化合物を付加反応させて得られる多価(メタ)アクリレート;メチレンビス(メタ)アクリルアミド等の多価(メタ)アクリルアミド;ジビニルベンゼン等の多価ビニル化合物;等を挙げることができる。 Specific examples of the ethylenically unsaturated compound having two or more ethylenically unsaturated bonds include alkyldiol di (meth) acrylates such as 1,9-nonanediol di (meth) acrylate; diethylene glycol di (meth) acrylate Such as polyethylene glycol di (meth) acrylate; polypropylene glycol di (meth) acrylate such as dipropylene glycol di (meth) acrylate; trimethylolpropane tri (meth) acrylate, pentaerythritol tri (meth) acrylate, and pentaerythritol tetra (meth) acrylate. A) Acrylate, glycerol tri (meth) acrylate, ethylene glycol diglycidyl ether and a compound having an ethylenically unsaturated bond and active hydrogen such as unsaturated carboxylic acid or unsaturated alcohol A polyvalent (meth) acrylate obtained by the reaction; a polyvalent (meth) acrylate obtained by an addition reaction of an unsaturated epoxy compound such as glycidyl (meth) acrylate and a compound having active hydrogen such as a carboxylic acid or an amine; Polyvalent (meth) acrylamides such as methylenebis (meth) acrylamide; polyvalent vinyl compounds such as divinylbenzene; and the like.
 現像疲労液に含んでいてもよい重合性化合物の濃度は特に限定されないが、30.0質量%以下であることが好ましく、15.0質量%以下であることがより好ましい。 (4) The concentration of the polymerizable compound that may be contained in the developing fatigue solution is not particularly limited, but is preferably 30.0% by mass or less, more preferably 15.0% by mass or less.
 <重合禁止剤>
 現像疲労液に含んでいてもよい重合禁止剤としては、具体的には、例えば、ハイドロキノンモノメチルエーテル、p-メトキシフェノール、ジ-t-ブチル-p-クレゾール、ピロガロール、t-ブチルカテコール、ベンゾキノン、4,4´-チオビス(3-メチル-6-t-ブチルフェノール)、2,2´-メチレンビス(4-メチル-6-t―ブチルフェノール)、N-ニトロソフェニルヒドロキシアミン第一セリウム塩等が挙げられる。
<Polymerization inhibitor>
Specific examples of the polymerization inhibitor which may be contained in the development fatigue solution include, for example, hydroquinone monomethyl ether, p-methoxyphenol, di-t-butyl-p-cresol, pyrogallol, t-butylcatechol, benzoquinone, 4,4'-thiobis (3-methyl-6-t-butylphenol), 2,2'-methylenebis (4-methyl-6-t-butylphenol), cerium N-nitrosophenylhydroxyamine, etc. .
 現像疲労液に含んでいてもよい重合禁止剤の濃度は特に限定されないが、0.3質量%以下であることが好ましく、0.15質量%以下であることがより好ましい。 (4) The concentration of the polymerization inhibitor that may be contained in the developing fatigue solution is not particularly limited, but is preferably 0.3% by mass or less, more preferably 0.15% by mass or less.
 <可塑剤>
 現像疲労液に含んでいてもよい可塑剤としては、例えば、液状ゴム、オイル、ポリエステル、およびリン酸系化合物等が挙げられる。
 液状ゴムとしては、具体的には、例えば、液状のポリブタジエン、液状のポリイソプレン、およびこれらをマレイン酸またはエポキシ基により変性したもの等が挙げられる。
 オイルとしては、具体的には、例えば、パラフィン、ナフテンおよびアロマ等が挙げられる。
 ポリエステルとしては、具体的には、例えば、アジピン酸系ポリエステル等が挙げられる。
 リン酸系化合物としては、具体的には、例えば、リン酸エステル等が挙げられる。
<Plasticizer>
Examples of the plasticizer that may be contained in the developing fatigue liquid include liquid rubber, oil, polyester, and a phosphoric acid compound.
Specific examples of the liquid rubber include liquid polybutadiene, liquid polyisoprene, and rubber modified with maleic acid or an epoxy group.
Specific examples of the oil include paraffin, naphthene and aroma.
Specific examples of the polyester include, for example, adipic acid-based polyester and the like.
Specific examples of the phosphoric acid compound include a phosphoric ester.
 現像疲労液に含んでいてもよい可塑剤の濃度は特に限定されないが、30質量%以下であることが好ましく、15質量%以下であることがより好ましい。 (4) The concentration of the plasticizer that may be contained in the developing fatigue solution is not particularly limited, but is preferably 30% by mass or less, and more preferably 15% by mass or less.
 <洗い出し液>
 現像疲労液に含まれる洗い出し液は、水系の洗い出し液であることが好ましく、水のみからなる液であってもよく、また、水を50質量%以上含有し、水に可溶な化合物を添加した水溶液であってもよい。水に可溶な化合物としては、界面活性剤、酸、アルカリ等が挙げられる。
<Washing liquid>
The washing solution contained in the developing fatigue solution is preferably an aqueous washing solution, and may be a solution consisting only of water, or containing a water-soluble compound containing at least 50% by mass of water. Aqueous solution may be used. Examples of the compound soluble in water include a surfactant, an acid, and an alkali.
 界面活性剤としては、アニオン系界面活性剤、ノニオン系界面活性剤、カチオン系界面活性剤、および両性系界面活性剤が挙げられ、なかでも、アニオン系界面活性剤が好ましい。
 アニオン性界面活性剤としては、具体的には、ラウリン酸ナトリウム、オレイン酸ナトリウム等の脂肪族カルボン酸塩;ラウリル硫酸エステルナトリウム、セチル硫酸エステルナトリウム、オレイル硫酸エステルナトリウム等の高級アルコール硫酸エステル塩;ポリオキシエチレンラウリルエーテル硫酸エステルナトリウム等のポリオキシエチレンアルキルエーテル硫酸エステル塩;ポリオキシエチレンオクチルフェニルエーテル硫酸エステルナトリウム、ポリオキシエチレンノニルフェニルエーテル硫酸エステルナトリウム等のポリオキシエチレンアルキルアリルエーテル硫酸エステル塩;アルキルジフェニルエーテルジスルホン酸塩、ドデシルスルホン酸ナトリウム、ジアルキルスルホコハク酸ナトリウム等のアルキルスルホン酸塩;アルキルジスルホン酸塩、ドデシルベンゼンスルホン酸ナトリウム、ジブチルナフタレンスルホン酸ナトリウム、トリイソプロピルナフタレンスルホン酸ナトリウム等のアルキルアリルスルホン酸塩;ラウリルリン酸モノエステルジナトリウム、ラウリルリン酸ジエステルナトリウム等の高級アルコールリン酸エステル塩;ポリオキシエチレンラウリルエーテルリン酸モノエステルジナトリウム、ポリオキシエチレンラウリルエーテルリン酸ジエステルナトリウム等のポリオキシエチレンアルキルエーテルリン酸エステル塩;等が挙げられる。これらは単独で用いてもよいし、2種以上を併合して用いてもよい。なお、具体例としてナトリウム塩を挙げたが、特にナトリウム塩に限定されるものではなく、カルシウム塩またはアンモニア塩等でも同様の効果を得ることができる。
Examples of the surfactant include an anionic surfactant, a nonionic surfactant, a cationic surfactant, and an amphoteric surfactant. Among them, an anionic surfactant is preferable.
Specific examples of the anionic surfactant include aliphatic carboxylate such as sodium laurate and sodium oleate; higher alcohol sulfate such as sodium lauryl sulfate, sodium cetyl sulfate and sodium oleyl sulfate; Polyoxyethylene alkyl ether sulfates such as sodium polyoxyethylene lauryl ether sulfate; polyoxyethylene alkyl allyl ether sulfates such as sodium polyoxyethylene octyl phenyl ether sulfate and sodium polyoxyethylene nonyl phenyl ether sulfate; Alkyl sulfonates such as alkyl diphenyl ether disulfonate, sodium dodecyl sulfonate, sodium dialkyl sulfosuccinate; Alkyl allyl sulfonates such as kildisulfonate, sodium dodecylbenzenesulfonate, sodium dibutylnaphthalenesulfonate and sodium triisopropylnaphthalenesulfonate; higher alcohol phosphoric acids such as disodium lauryl monoester disodium and sodium lauryl diester sodium Ester salts; polyoxyethylene alkyl ether phosphoric acid ester salts such as disodium polyoxyethylene lauryl ether phosphate monoester and sodium polyoxyethylene lauryl ether phosphate; and the like. These may be used alone or in combination of two or more. In addition, although the sodium salt is mentioned as a specific example, it is not particularly limited to the sodium salt, and the same effect can be obtained by a calcium salt, an ammonium salt, or the like.
 ノニオン系界面活性剤としては、具体的には、ポリオキシエチレンオレイルエーテルまたはポリオキシエチレンラウリルエーテル等のポリオキシエチレンアルキルエーテル類、ポリオキシエチレンノニルフェニルエーテルまたはポリオキシエチレンオクチルフェニルエーテル等のポリオキシエチレンアルキルフェニルエーテル等、ポリオキシエチレンポリオキシプロピレングリコール類、ポリエチレングリコールモノステアレートまたはポリエチレングリコールモノオレートまたはポリエチレングリコールジラウレート等の脂肪酸とポリエチレングリコールとのモノおよびジエステル類、ソルビタンモノラウレートまたはソルビタンモノオレート等の脂肪酸とソルビタンのエステル類、ポリオキシエチレンソルビタンモノラウレートまたはリオキシエチレンソルビタンモノシテアレートまたはポリオキシエチレンソルビタントリラウレート等のソルビタンのポリオキシエチレン付加物と脂肪酸とのエステル類、ソルビットモノパルチミテートまたはソルビットジラウレート等の脂肪酸とソルビットとのエステル類、ポリオキシエチレンソルビットモノステアレートまたはポリオキシエチレンソルビットジオレート等のソルビットのポリオキシエチレン付加物と脂肪酸とのエステル類、ペンタエリスリトールモノステアレート等の脂肪酸とペンタエリスロトールとのエステル類,グリセリンモノラウレート等の脂肪酸とグリセリンとのエステル類、ラウリン酸ジエタノールアミドまたはラウリン酸モノエタノールアミド等の脂肪酸アルカノールアミド類、ラウリルジメチルアミンオキサイド等のアミンオキサイド類、ステアリルジエタノールアミン等の脂肪酸アルカノールアミン類、ポリオキシエチレンアルキルアミン類、トリエタノールアミン脂肪酸エステル類、リン酸塩、炭酸塩、ケイ酸塩等のアルカリ性を示す塩化合物が挙げられる。これらは単独で用いてもよいし、2種以上を併合して用いてもよい。 Specific examples of the nonionic surfactant include polyoxyethylene alkyl ethers such as polyoxyethylene oleyl ether and polyoxyethylene lauryl ether, and polyoxyethylene nonyl phenyl ether and polyoxyethylene such as polyoxyethylene octyl phenyl ether. Mono- and diesters of fatty acids such as ethylene alkyl phenyl ether, polyoxyethylene polyoxypropylene glycols, polyethylene glycol monostearate or polyethylene glycol monooleate or polyethylene glycol dilaurate with polyethylene glycol, sorbitan monolaurate or sorbitan monooleate Esters of sorbitan with fatty acids such as, polyoxyethylene sorbitan monolaurate or Esters of polyoxyethylene adducts of sorbitan such as oxyethylene sorbitan monocitrate or polyoxyethylene sorbitan trilaurate with fatty acids, esters of fatty acids with sorbite such as sorbit monopartitate or sorbit dilaurate, polyoxy Esters of fatty acids such as ethylene sorbit monostearate or polyoxyethylene sorbite diolate and fatty acids, such as pentaerythritol monostearate, esters of pentaerythritol and fatty acids, glycerin monolaurate, etc. Esters of fatty acids with glycerin, fatty acid alkanolamides such as lauric acid diethanolamide or lauric acid monoethanolamide, lauryl dimethylamine Amine compounds such as side oxides, fatty acid alkanolamines such as stearyldiethanolamine, polyoxyethylene alkylamines, triethanolamine fatty acid esters, phosphates, carbonates, and salt compounds showing alkalinity such as silicates. . These may be used alone or in combination of two or more.
 カチオン系界面活性剤としては、具体的には、モノステアリルアンモニウムクロライド、ジステアリルアンモニウムクロライド、トリステアリルアンモニウムクロライド等の1級および2級および3級アミン塩類、ステアリルトリメチルアンモウムクロライド、ジステアリルジメチルアンモニウムクロライド、ステアリルジメチルベンジルアンモニウムクロライド等の4級アンモニウム塩類、N―セチルピリジニウムクロライドまたはN-ステアリルピリジニウムクロライド等のアルキルピリジニウム塩類、N,Nジアルキルモルホリニウム塩類、ポリエチレンポリアミンの脂肪酸アミド塩類、アミノエチルエタノールアミンとステアリン酸とのアミドの尿素化合物の酢酸塩類、2-アルキル-1-ヒドロキシエチルイミダゾリニウムクロライド等が挙げられる。これらは単独で用いてもよいし、2種以上を併合して用いてもよい。 Specific examples of the cationic surfactant include primary, secondary and tertiary amine salts such as monostearyl ammonium chloride, distearyl ammonium chloride and tristearyl ammonium chloride, stearyl trimethylammonium chloride, distearyl dimethyl ammonium. Quaternary ammonium salts such as chloride, stearyldimethylbenzylammonium chloride, alkylpyridinium salts such as N-cetylpyridinium chloride or N-stearylpyridinium chloride, N, N-dialkylmorpholinium salts, fatty acid amide salts of polyethylenepolyamine, aminoethylethanol Acetates of urea compounds of amides of amines and stearic acid, 2-alkyl-1-hydroxyethylimidazolinium chloride Ido, and the like. These may be used alone or in combination of two or more.
 両性系界面活性剤としては、具体的には、ラウリルアミンプロピオン酸ソーダ等のアミノ酸型、ラウリルジメチルベタインまたはラウリルジヒドキシエチルベタイン等のカルボキシベタイン型、ステアリルジメチルスルホエチレンアンモニウムエチレンアンモニウムベタイン等のスルホベタイン型、イミダゾリニウムベタイン型、レスチン等が挙げられる。これらは単独で用いてもよいし、2種以上を併合して用いてもよい。 Specific examples of the amphoteric surfactant include an amino acid type such as sodium laurylamine propionate, a carboxy betaine type such as lauryl dimethyl betaine or lauryl dihydroxyethyl betaine, and a sulfo acid such as stearyl dimethyl sulfoethylene ammonium ethylene ammonium betaine. Betaine type, imidazolinium betaine type, restin and the like. These may be used alone or in combination of two or more.
 酸としては、具体的には、例えば、塩酸、硫酸、硝酸、リン酸、ギ酸、酢酸、シュウ酸、コハク酸、クエン酸、リンゴ酸、マレイン酸、パラトルエンスルホン酸等の無機酸または有機酸が挙げられる。
 アルカリとしては、具体的には、例えば、水酸化リチウム、水酸化ナトリウム、水酸化マグネシウム、水酸化カリウム、水酸化カルシウム、酸化カルシウム、炭酸ナトリウム、炭酸水素ナトリウム、炭酸カルシウム等が挙げられる。
Specific examples of the acid include inorganic or organic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, formic acid, acetic acid, oxalic acid, succinic acid, citric acid, malic acid, maleic acid, and paratoluenesulfonic acid. Is mentioned.
Specific examples of the alkali include lithium hydroxide, sodium hydroxide, magnesium hydroxide, potassium hydroxide, calcium hydroxide, calcium oxide, sodium carbonate, sodium hydrogen carbonate, calcium carbonate and the like.
 本発明は、基本的に以上のように構成されるものである。以上、本発明の処理方法および処理装置について詳細に説明したが、本発明は上述の実施形態に限定されず、本発明の主旨を逸脱しない範囲において、種々の改良または変更をしてもよいのはもちろんである。 The present invention is basically configured as described above. As described above, the processing method and the processing apparatus of the present invention have been described in detail. However, the present invention is not limited to the above embodiments, and various improvements or changes may be made without departing from the gist of the present invention. Of course.
 以下に実施例を挙げて本発明の特徴をさらに具体的に説明する。以下の実施例に示す材料、試薬、物質量とその割合、および、操作等は本発明の趣旨から逸脱しない限り適宜変更することができる。従って、本発明の範囲は以下の実施例に限定されるものではない。
 本実施例では、以下に示す実施例1、2および比較例1、2の処理装置を用いて、下記表1に示す処理量の現像疲労液について処理を行った。
 実施例1、2および比較例1、2では、回収した固形物量と、排出した固形物の含水率を測定した。回収した固形物量および排出した固形物の含水率の結果を下記表1に示す。
Hereinafter, the features of the present invention will be described more specifically with reference to examples. Materials, reagents, substance amounts and their ratios, operations, and the like shown in the following examples can be appropriately changed without departing from the spirit of the present invention. Therefore, the scope of the present invention is not limited to the following examples.
In this example, processing was performed on the developing fatigue liquid having the processing amount shown in Table 1 below using the processing apparatuses of Examples 1 and 2 and Comparative Examples 1 and 2 shown below.
In Examples 1 and 2 and Comparative Examples 1 and 2, the amount of collected solids and the water content of the discharged solids were measured. The results of the amount of collected solids and the moisture content of the discharged solids are shown in Table 1 below.
 実施例1、2および比較例1、2で処理される現像疲労液を得るために使用する装置および薬品を以下に示す。
<イメージング機>
・CDI Spark 4835 Inline(ESKO社製)
<露光機>
・紫外線露光機 Concept 302 ECDLF(製品名)(Glunz&Jensen社製)
<現像機>
・SB-926(GS Trading社製)
<感光性樹脂版>
・FLENEX FW-L(富士フイルムグローバルグラフィックシステムズ社製)
<洗い出し液>
・フィニッシュパワー&ピュアパウダーSP(レキット・ベンキーザージャパン社製)の水溶液(濃度は0.5質量%) 200リットル
<遠心分離機>
・UB-S1(株式会社アメロイド日本サービス社製)
The equipment and chemicals used to obtain the developing fatigue solutions processed in Examples 1 and 2 and Comparative Examples 1 and 2 are shown below.
<Imaging machine>
・ CDI Spark 4835 Inline (manufactured by ESKO)
<Exposure machine>
-UV exposure machine Concept 302 ECDLF (product name) (Glunz & Jensen)
<Developer>
・ SB-926 (manufactured by GS Trading)
<Photosensitive resin plate>
・ FLENEX FW-L (manufactured by FUJIFILM Global Graphic Systems)
<Washing liquid>
・ Finish Power & Pure Powder SP (manufactured by Rekit Benkeiser Japan) aqueous solution (concentration: 0.5% by mass) 200 liters <Centrifuge>
・ UB-S1 (Ameloid Japan Service Co., Ltd.)
<現像疲労液の調製>(実施例1、2および比較例1、2)
 上述の感光性樹脂版に対して、上述の紫外線露光機を用いて、感光性樹脂版の裏面から80Wのエネルギーで10秒間露光することにより裏露光を実施した。その後、上述のイメージング機を用いて、マスク層をアブレーションすることでイメージングし、表面(裏面の裏面)から80Wで1000秒間露光することにより主露光を実施した。
 主露光した感光性樹脂版に対し、上述の洗い出し液と、洗出し機SB-926を用いて、50℃の条件で、ブラシを用いて現像することにより未露光部を除去し、現像疲労液を得た。
<Preparation of developer fatigue solution> (Examples 1 and 2 and Comparative Examples 1 and 2)
The above-mentioned photosensitive resin plate was exposed from the back surface of the photosensitive resin plate with an energy of 80 W for 10 seconds using the above-mentioned ultraviolet exposure machine to perform back exposure. Thereafter, using the above-described imaging machine, imaging was performed by ablating the mask layer, and main exposure was performed by exposing from the front surface (back surface of the back surface) at 80 W for 1000 seconds.
The main-exposed photosensitive resin plate is developed with the above-mentioned washing solution and a washing machine SB-926 at 50 ° C. using a brush to remove unexposed portions, and a developing fatigue solution I got
<回収した固形物量の測定方法>
 測定対象の現像疲労液の一定量をアルミニウム容器にとり、温度95℃で12時間乾燥させた。
 乾燥前の一定量の現像疲労液の質量と、一定量の現像疲労液を乾燥した後の質量とを測定した。そして、乾燥前後の質量差に基づき、固形物量を計算した。この固形物量を、回収した固形物量とした。その結果を下記表1の回収した固形物量(濃度100%として)の欄に記載した。
<Method for measuring the amount of collected solids>
A fixed amount of the developing fatigue solution to be measured was placed in an aluminum container and dried at a temperature of 95 ° C. for 12 hours.
The mass of a certain amount of developing fatigue solution before drying and the mass after drying a certain amount of developing fatigue solution were measured. Then, the amount of solids was calculated based on the difference in mass before and after drying. This solid content was taken as the collected solid content. The results are shown in the column of the amount of collected solids (concentration: 100%) in Table 1 below.
<排出した固形物の含水率の測定方法>
 排出した固形物の含水率には乾燥重量法を用いた。サンプルを加熱オーブンに入れて乾燥させ、乾燥後の含水率を0%として、サンプルの乾燥前後の重量から含水率を求めた。その結果を下記表1の排出した固形物の含水率(質量%)の欄に記載した。
<Method of measuring moisture content of discharged solid>
The dry weight method was used for the moisture content of the discharged solid. The sample was placed in a heating oven and dried. The moisture content after drying was set to 0%, and the moisture content was determined from the weight of the sample before and after drying. The results are shown in the column of moisture content (% by mass) of the discharged solid in Table 1 below.
 次に、実施例1、2および比較例1、2について説明する。
 (実施例1)
 実施例1は、上述の現像疲労液を、図1に示す構成の処理装置を用いて処理した。実施例1では、回転する容器へ現像疲労液の供給を停止し、一定時間の間(3分間)、容器の回転を継続した後、容器の回転を停止する動作を行った。この動作のことを第1の動作という。なお、容器内の固形物の除去には、スクレーパーと圧縮エアー噴出を用いた。
 下記表1の遠心分離の欄に示す「2500rpm 5L/分」において、「2500rpm」は遠心分離の際の回転数を示す。「5L/分(リットル/分)」は現像疲労液を遠心分離機に送る流量を示す。
 下記表1の処理量とは、感光性樹脂版を何平米(m)、現像処理したかを示すものであり、現像処理した感光性樹脂版の総面積(m)を表すものである。
 (実施例2)
 実施例2は、実施例1に比して、図10に示す構成の処理装置を用いて処理した点、および第1の動作に加えて、第2の動作を実施した点が異なり、それ以外は実施例1と同じとした。
 第2の動作は、容器を回転させながら貯留槽内の現像疲労液の一部を容器に戻した後、容器内に貯留された現像疲労液と共に、遠心分離を実施する動作のことである。
 実施例2では、回収した固形物量は、第1の動作と第2の動作とにより得られたものである。
Next, Examples 1 and 2 and Comparative Examples 1 and 2 will be described.
(Example 1)
In Example 1, the above-mentioned developing fatigue solution was processed using the processing apparatus having the configuration shown in FIG. In Example 1, the operation of stopping the supply of the developing fatigue solution to the rotating container, continuing the rotation of the container for a certain period of time (3 minutes), and then stopping the rotation of the container was performed. This operation is called a first operation. In addition, a scraper and a compressed air jet were used for removing solid matter in the container.
In "2500 rpm 5 L / min" shown in the column of centrifugation in Table 1 below, "2500 rpm" indicates the number of revolutions at the time of centrifugation. “5 L / min (liter / min)” indicates a flow rate at which the developing fatigue solution is sent to the centrifuge.
The processing amount shown in Table 1 below indicates how many square meters (m 2 ) of the photosensitive resin plate has been developed, and indicates the total area (m 2 ) of the developed photosensitive resin plate. .
(Example 2)
The second embodiment is different from the first embodiment in that processing is performed using the processing apparatus having the configuration shown in FIG. 10 and that the second operation is performed in addition to the first operation. Was the same as in Example 1.
The second operation is an operation of returning a part of the developing fatigue liquid in the storage tank to the container while rotating the container, and then performing centrifugal separation together with the developing fatigue liquid stored in the container.
In the second embodiment, the amount of collected solids is obtained by the first operation and the second operation.
 (比較例1)
 比較例1は、実施例1に比して、図12に示す構成のキーパーディスクがない処理装置を用いた点、および遠心分離した後、再度容器を回転させていない点が異なり、それ以外は実施例1と同じとした。
 (比較例2)
 比較例2は、比較例1に比して、処理量が異なり、それ以外は比較例1と同じとした。
(Comparative Example 1)
Comparative Example 1 is different from Example 1 in that a processing apparatus without the keeper disk having the configuration shown in FIG. 12 was used and that the container was not rotated again after centrifugation. Same as Example 1.
(Comparative Example 2)
Comparative Example 2 was the same as Comparative Example 1 except that the processing amount was different from that of Comparative Example 1.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 表1に示すように、実施例1、2は、比較例1、2に比して、回収した固形物量が多く、かつ排出した固形物の含水率を少なくできた。
 処理量が同じ実施例1、2と比較例2とを比べても、実施例1、2の方が回収した固形物量が多かった。
 実施例1、2から、実施例2は、排出された現像疲労液に対して再度処理することにより、実施例1よりも固形物量を多く回収することができた。
As shown in Table 1, in Examples 1 and 2, compared with Comparative Examples 1 and 2, the amount of collected solids was large, and the water content of the discharged solids could be reduced.
Even when Examples 1 and 2 and Comparative Example 2 having the same treatment amount were compared, Examples 1 and 2 showed a larger amount of collected solids.
From Examples 1 and 2, Example 2 was able to recover a larger amount of solids than Example 1 by treating the discharged developer fatigue solution again.
 10、10a、10b、10c、100 処理システム
 12、102 処理装置
 14 現像装置
 20 容器
 20a 胴部
 20b 傾斜部
 20c 底部
 20d 底面
 20e 開口
 20f 開口部
 20g 内壁
 21a 蓋
 21b 開口部
 21d 排出路
 21c シャッター
 22 インサイドディスク
 22a 開口
 23、60 キーパーディスク
 24 ケース
 25 排出路
 26 駆動部
 27 消泡タンク
 28、31 配管
 29 ポンプ
 30 分離膜
 31a 開口
 32 受皿
 33 除去部
 34 スクレーパー
 35a 駆動軸
 35b 駆動ギア
 35c 従動ギア
 36 第1の固形物
 37 第2の固形物
 38 制御部
 40 現像槽
 42 ブラシ
 43 駆動部材
 44 供給管
 46 供給部
 47 バルブ
 50 感光性樹脂版
 50a 表面
 60a 開口
 60b 本体部
 70 貯留槽
 71、73 配管
 72、82 ポンプ
 73a、83a 開口
 74 供給部
 75、81、83 配管
 84 送液部
 104 内面
 C 中心軸
 Q 洗い出し液
 Qw 現像疲労液
 R 方向
 r 方向
10, 10a, 10b, 10c, 100 Processing system 12, 102 Processing device 14 Developing device 20 Container 20a Body 20b Inclined portion 20c Bottom 20d Bottom surface 20e Opening 20f Opening 20g Inner wall 21a Cover 21b Opening 21d Drain 21c Shutter 22 Inside Disk 22a Opening 23, 60 Keeper disk 24 Case 25 Discharge path 26 Drive unit 27 Defoaming tank 28, 31 Piping 29 Pump 30 Separation membrane 31a Opening 32 Receiving tray 33 Removing unit 34 Scraper 35a Drive shaft 35b Drive gear 35c Follower gear 36 First Of solid 37 Second solid 38 Control part 40 Developing tank 42 Brush 43 Drive member 44 Supply pipe 46 Supply part 47 Valve 50 Photosensitive resin plate 50a Surface 60a Opening 60b Body part 70 Storage tank 71, 73 72 and 82 pumps 73a, 83a opening 74 supplying portions 75,81,83 pipe 84 feeding portion 104 inner surface C central axis Q washout solution Qw developer fatigued solution R direction r direction

Claims (9)

  1.  洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液について、前記固形物を除去する処理方法であって、
     前記現像疲労液を容器内に供給しながら、前記容器を回転し、前記現像疲労液に含まれる固形物を遠心分離し、
     その後、前記現像疲労液の供給を停止し、一定時間の間、前記容器の回転を継続した後、前記容器の回転を停止する、処理方法。
    A processing method for removing the solid matter, with respect to a developing fatigue liquid containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washout liquid, ,
    While supplying the developing fatigue solution into the container, rotating the container, centrifuging the solids contained in the developing fatigue solution,
    Thereafter, the supply of the developing fatigue solution is stopped, and after the rotation of the container is continued for a predetermined time, the rotation of the container is stopped.
  2.  洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液について、前記洗い出し液よりも比重の小さい第1の固形物と、前記洗い出し液よりも比重の大きい第2の固形物とを除去する処理方法であって、
     回転する容器内へ前記現像疲労液を供給し、前記現像疲労液に含まれる前記第1の固形物と前記第2の固形物とを遠心分離し、前記第2の固形物を前記容器の内壁に集積し、前記第1の固形物を前記容器内に設けられた保持部材に集積させる第1の工程と、
     回転する前記容器への前記現像疲労液の供給を停止し、一定時間の間、前記容器の回転を継続する第2の工程と、
     前記第1の固形物が前記保持部材に保持された状態で、前記容器の回転を停止する第3の工程と、
     前記容器を回転させて、前記保持部材に保持された前記第1の固形物を、前記保持部材から取り除く第4の工程とを有する、請求項1に記載の処理方法。
    By the development using the washing liquid, the first fatigue having a specific gravity smaller than that of the washing liquid is used for the developing fatigue liquid containing solid matter generated by removing the unexposed portion of the photosensitive resin plate after imagewise exposure. A processing method for removing a solid and a second solid having a specific gravity greater than that of the washing liquid,
    Supplying the developing fatigue solution into a rotating container, centrifuging the first solid material and the second solid material contained in the developing fatigue solution, and removing the second solid material from the inner wall of the container; A first step of accumulating the first solid matter on a holding member provided in the container;
    A second step of stopping the supply of the developing fatigue solution to the rotating container and continuing to rotate the container for a predetermined time;
    A third step of stopping the rotation of the container while the first solid is held by the holding member;
    The method according to claim 1, further comprising: a fourth step of rotating the container to remove the first solid held by the holding member from the holding member.
  3.  前記第4の工程の後に、前記容器から排出された前記現像疲労液の一部を前記容器に戻し、前記容器を回転させて前記容器内の前記現像疲労液を前記遠心分離し、前記第1の固形物を前記保持部材に集積させた後、前記容器内の前記現像疲労液を前記容器内から排出し、
     次に、前記保持部材に集積された前記第1の固形物が前記保持部材に保持された状態で、前記容器の回転を停止した後、再度、前記容器を回転させる、請求項2に記載の処理方法。
    After the fourth step, a part of the developing fatigue solution discharged from the container is returned to the container, and the container is rotated to centrifuge the developing fatigue solution in the container, and the first After the solid matter is accumulated on the holding member, the developing fatigue solution in the container is discharged from the container,
    Next, after stopping the rotation of the container while the first solid matter accumulated on the holding member is held by the holding member, the container is rotated again. Processing method.
  4.  前記第4の工程の後に、前記第1の固形物と前記第2の固形物とを同時に前記容器から除去する工程を有する、請求項2または3に記載の処理方法。 4. The processing method according to claim 2, further comprising, after the fourth step, a step of simultaneously removing the first solid and the second solid from the container.
  5.  前記容器から排出された前記現像疲労液を前記洗い出し液として再使用する工程を有する、請求項2~4のいずれか1項に記載の処理方法。 (5) The processing method according to any one of (2) to (4), further comprising a step of reusing the developing fatigue solution discharged from the container as the washing solution.
  6.  洗い出し液を用いた現像によって、画像様露光後の感光性樹脂版の未露光部が除去されることにより発生する固形物を含んだ現像疲労液を貯留する、開口部を有する容器と、
     前記容器を回転させて前記洗い出し液よりも比重の小さい第1の固形物と、前記洗い出し液よりも比重の大きい第2の固形物とを前記容器内で遠心分離させる駆動部と、
     前記容器内、かつ前記開口部に面して設けられ、前記第1の固形物を前記容器内に留める規制部材と、
     前記容器内、かつ前記規制部材に対して前記開口部とは反対側に、少なくとも1つ設けられた、前記遠心分離により集積される前記第1の固形物を保持する保持部材とを有し、
     前記駆動部により前記現像疲労液が貯留された前記容器を回転させて遠心分離し、前記第1の固形物を前記保持部材に集積させた後、回転する前記容器への前記現像疲労液の供給を停止し、一定時間の間、前記容器の回転を継続し、さらにその後、前記保持部材に集積された前記第1の固形物が前記保持部材に保持された状態で、前記駆動部による前記容器の回転を停止した後、再度、前記駆動部により前記容器を回転させる制御部とを有する、処理装置。
    A container having an opening, storing a development fatigue solution containing a solid matter generated by removing an unexposed portion of the photosensitive resin plate after imagewise exposure by development using a washing liquid,
    A first solid that has a lower specific gravity than the wash liquid by rotating the container, and a second solid that has a higher specific gravity than the wash liquid, and a driving unit that centrifugally separates the second solid within the container.
    A regulating member provided in the container, and facing the opening, for retaining the first solid substance in the container;
    In the container, and on the opposite side to the opening with respect to the regulating member, at least one provided, a holding member for holding the first solid matter accumulated by the centrifugation,
    The drive unit rotates the container in which the developing fatigue liquid is stored, centrifugally separates the liquid, accumulates the first solid matter on the holding member, and supplies the developing fatigue liquid to the rotating container. Is stopped, and the rotation of the container is continued for a certain period of time. Further, in a state where the first solid matter accumulated on the holding member is held by the holding member, the container is driven by the driving unit. And a control unit for rotating the container again by the driving unit after stopping the rotation of the processing unit.
  7.  前記容器から排出された前記現像疲労液を貯留し、かつ排出された前記現像疲労液の一部を前記容器に戻す供給部を備える貯留槽を有し、
     前記供給部により、前記容器から排出された前記現像疲労液の一部を前記容器に戻した後、
     前記制御部は、前記駆動部により前記容器を回転させて前記容器内の前記現像疲労液を前記遠心分離し、前記第1の固形物を前記保持部材に集積させた後、前記容器内の前記現像疲労液を前記容器内から排出し、
     次に、前記保持部材に集積された前記第1の固形物が前記保持部材に保持された状態で、前記駆動部による前記容器の回転を停止した後、再度、前記駆動部により前記容器を回転させる、請求項6に記載の処理装置。
    A storage tank having a supply unit for storing the developing fatigue liquid discharged from the container and returning a part of the discharged developing fatigue liquid to the container,
    By the supply unit, after returning a part of the developing fatigue solution discharged from the container to the container,
    The control unit is configured to rotate the container by the driving unit to centrifuge the developing fatigue solution in the container, and to accumulate the first solid matter in the holding member. Draining the developer fatigue solution from the container;
    Next, after the rotation of the container by the driving unit is stopped in a state where the first solid matter accumulated on the holding member is held by the holding member, the container is again rotated by the driving unit. The processing apparatus according to claim 6, wherein the processing is performed.
  8.  前記容器内に存在する前記第1の固形物および前記第2の固形物を前記容器から除去する除去部を有する、請求項6または7に記載の処理装置。 8. The processing apparatus according to claim 6, further comprising a removing unit configured to remove the first solid and the second solid present in the container from the container. 9.
  9.  前記容器から排出された前記現像疲労液を、前記洗い出し液として再使用する循環部を有する、請求項6~8のいずれか1項に記載の処理装置。 The processing apparatus according to any one of claims 6 to 8, further comprising a circulation unit for reusing the developing fatigue solution discharged from the container as the washing solution.
PCT/JP2019/026629 2018-07-27 2019-07-04 Processing method and processing device WO2020022019A1 (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01228129A (en) * 1988-03-09 1989-09-12 Tokyo Electron Ltd Development device
JPH10123722A (en) * 1996-10-21 1998-05-15 Nippon Zeon Co Ltd Developing device for photosensitive original printing plate
WO2018180252A1 (en) * 2017-03-31 2018-10-04 富士フイルム株式会社 Treatment method and treatment device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01228129A (en) * 1988-03-09 1989-09-12 Tokyo Electron Ltd Development device
JPH10123722A (en) * 1996-10-21 1998-05-15 Nippon Zeon Co Ltd Developing device for photosensitive original printing plate
WO2018180252A1 (en) * 2017-03-31 2018-10-04 富士フイルム株式会社 Treatment method and treatment device

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