WO2004029140A1 - Volume-decreased gel-like polystyrene resin separating and recovering device - Google Patents

Volume-decreased gel-like polystyrene resin separating and recovering device Download PDF

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Publication number
WO2004029140A1
WO2004029140A1 PCT/JP2002/010098 JP0210098W WO2004029140A1 WO 2004029140 A1 WO2004029140 A1 WO 2004029140A1 JP 0210098 W JP0210098 W JP 0210098W WO 2004029140 A1 WO2004029140 A1 WO 2004029140A1
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WO
WIPO (PCT)
Prior art keywords
resin
volume
heat medium
gel
polystyrene resin
Prior art date
Application number
PCT/JP2002/010098
Other languages
French (fr)
Japanese (ja)
Inventor
Shigenobu Hamano
Noriomi Hayashi
Original Assignee
Meishin Kogyo Kabushikigaisha
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 Meishin Kogyo Kabushikigaisha filed Critical Meishin Kogyo Kabushikigaisha
Priority to PCT/JP2002/010098 priority Critical patent/WO2004029140A1/en
Priority to AU2002332344A priority patent/AU2002332344A1/en
Priority to US10/529,482 priority patent/US7666368B2/en
Priority to AU2003268682A priority patent/AU2003268682A1/en
Priority to JP2005501952A priority patent/JP4379813B2/en
Priority to PCT/JP2003/012310 priority patent/WO2004029113A1/en
Priority to AT03748594T priority patent/ATE489213T1/en
Priority to DE60335126T priority patent/DE60335126D1/en
Priority to EP20030748594 priority patent/EP1550676B1/en
Priority to TW92126905A priority patent/TWI311572B/en
Publication of WO2004029140A1 publication Critical patent/WO2004029140A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0293Dissolving the materials in gases or liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2025/00Use of polymers of vinyl-aromatic compounds or derivatives thereof as moulding material
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to a technique for recovering a liquid (solvent) and a resin from a volume-reduced gel polystyrene resin, and more particularly to a volume-reduced gel for continuously separating and recovering a solvent and a resin from a volume-reduced gel polystyrene resin.
  • the present invention relates to an apparatus for separating and collecting a polystyrene resin.
  • Japanese Patent Application Laid-Open No. 2001-181439 discloses a dissolving tank for preparing a dissolving solution by adding a solvent to a gel obtained by dissolving polystyrene in a solvent, and filtering the dissolving solution.
  • a polystyrene recovery device comprising a filter, a concentrator for evaporating the solvent from the solution passed through the filter to produce a concentrated solution having a predetermined concentration, and a separator for evaporating and separating the solvent from the concentrated solution to take out polystyrene. Proposed.
  • the separator of such a device is a thin-film evaporation type separator 90, which is a double-structured container composed of a separator inner cylinder 91 and a separator outer cylinder 92. Heat is circulated between the heat exchangers 92 and heats the concentrate, and the concentrated liquid is introduced along the inner cylinder 92. In this case, the introduced concentrated liquid flows down along the inner cylinder 92 while the solvent gradually evaporates. However, when the resin concentration becomes high, the concentrated liquid does not flow down. However, the resin adhering to the inner cylinder 92 is scraped off by a scraping plate 97 provided via 6 However, the above-described conventional separator for separating the resin and the solvent is generally used.
  • the present invention has been made in view of the above circumstances, and provides a volume-reduced gel polystyrene resin separation and recovery apparatus for continuously and efficiently treating a volume-reduced gel polystyrene resin to separate and recover a solvent and a resin. As an issue.
  • a first aspect of the present invention that solves the above-mentioned problem is that a reduced volume gel-like polystyrene resin
  • a separation / recovery device that separates and recovers a solvent and a resin by heating under normal pressure or reduced pressure.
  • An apparatus main body having a resin recovery section to be recovered at a lower portion, a heat medium flow pipe arranged in the apparatus main body and flowing a heat medium inward, and a volume reduced so as to contact the heat medium flow pipe.
  • a gel resin introduction means for introducing a gel-like polystyrene resin, a resin holding portion provided at a lower portion of the apparatus main body for holding a resin that has flowed downward in contact with the heat medium flow pipe, and a resin holding portion provided with the resin holding portion.
  • the resin and the solvent can be separated and recovered, and the treatment efficiency can be significantly improved.
  • the heat medium flow pipe is spirally arranged near the peripheral wall of the apparatus main body so as to be multilayered in a vertical direction.
  • a volume-reduced gel-like polystyrene resin separation and recovery device In a volume-reduced gel-like polystyrene resin separation and recovery device.
  • the volume-reduced gel-like polystyrene resin is heated by coming into contact with the heat medium flow tube, and the solvent is efficiently separated and removed from the volume-reduced gel-like polystyrene resin.
  • the volume-reduced gel-like polystyrene resin that has come into contact with the heat medium flow tube flows along the heat medium flow tube and is disposed above the heat medium flow tube.
  • a volume-reduced gel-like polystyrene resin separation / recovery device characterized by flowing down from a medium flow tube to a heat medium flow tube arranged below and moving to the resin holding section.
  • the period during which the volume-reduced gel-like polystyrene resin is in contact with the heat medium flow tube is lengthened, and the solvent can be efficiently and reliably removed from the volume-reduced gel-like polystyrene resin.
  • the volume-reducing tube which flows in contact with the heat medium flow pipe at a predetermined interval in the vicinity of the heat medium flow pipe.
  • a flow control plate for guiding the flow of the polystyrene resin is provided along the heat medium flow pipe.
  • the volume-reduced gel-like polystyrene resin flowing from the heat medium flow tube surely comes into contact with the heat medium flow tube disposed below the flow control plate via the flow control plate.
  • the flow control plate below the lowermost layer of the heat medium flow pipe guides the resin flowing down from the heat medium flow pipe toward the wall surface of the apparatus main body.
  • the resin flowing down from the heat medium flow pipe flows into the resin holding portion via the wall surface of the apparatus main body heated by the heating means, so that the fluidity is secured without solidifying the resin. Is done.
  • the heating means includes a heat medium circulating means for circulating a heat medium along a lower wall surface of the apparatus main body.
  • a heat medium circulating means for circulating a heat medium along a lower wall surface of the apparatus main body.
  • the fluidity of the resin flowing on the wall surface of the apparatus main body can be more reliably maintained.
  • the heating means is provided in a substantially cylindrical shape provided so as to surround the stirrer provided in a substantially central bottom of the resin holding part.
  • a volume-reduced gel-like polystyrene resin separation / recovery device comprising a heat medium circulation path in a shape.
  • the resin in the resin holding portion is reliably maintained at the predetermined temperature at which the resin is heated, so that the resin can be prevented from solidifying, and the solvent remaining in the resin can be almost completely removed. .
  • the gel resin introducing means is disposed above the heat medium flow pipe and driven to rotate, and the gutter-shaped member is provided.
  • a volume-reduced gel-like polystyrene resin separation and recovery device characterized by flowing down.
  • the volume-reduced gel-polystyrene resin flows down from the gutter-like member onto the heat medium flow pipe in a substantially uniform amount over the circumferential direction of the apparatus main body.
  • the resin discharged from the resin recovery section is transferred in a substantially horizontal direction.
  • a pay-out pump is provided to collect the resin.
  • the resin discharged from the resin recovery section flows through the transfer pipe to reach the discharge pump, so that bubbles contained in the resin are significantly reduced.
  • an apparatus for separating and collecting a reduced volume gel-like polystyrene resin comprising heating means for heating the periphery of the transfer tube.
  • the resin flowing through the transfer tube is heated, and its fluidity is ensured.
  • FIG. 1 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
  • FIG. 2 is an enlarged view of a main part of the volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
  • FIG. 3 is a schematic diagram illustrating a separation and recovery procedure using a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
  • FIG. 4 is a schematic diagram illustrating a separation and recovery procedure using a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
  • FIG. 5 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation device according to Embodiment 1 of the present invention.
  • FIG. 6 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation device according to Embodiment 2 of the present invention.
  • FIG. 1 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation / recovery device according to Embodiment 1
  • FIG. 2 is a partially enlarged view of the volume-reduced gel-like polystyrene resin separation / recovery device.
  • the volume-reduced gel-like polystyrene resin separation and recovery apparatus of the present embodiment is for separating a resin and a solvent by heating the volume-reduced gel-like polystyrene resin under reduced pressure, and recovering them, respectively.
  • a solvent recovery unit 11 for continuously removing the evaporated solvent is provided on the upper surface of the cylindrical apparatus main body 10, and a resin for removing the solvent from which the solvent has been removed is provided on the bottom surface of the apparatus main body 10.
  • the lower part of the device main body 10 where the resin recovery section 12 is provided has a smaller outer diameter than the upper part, and holds the resin from which the solvent has been removed from the volume-reduced gel-like polystyrene resin, which will be described in detail later.
  • the resin holding portion 13 is formed.
  • the resin collecting section 12 is connected to the resin holding section 13.
  • an exhaust pipe (not shown) connected to a condenser (condenser) and a recovery tank is connected to the solvent recovery section 11. Then, the inside of the apparatus main body 10 is constantly sucked through the exhaust pipe to be in a reduced pressure state.
  • an introduction means for introducing the volume-reduced gel-like polystyrene resin into the apparatus main body 10 is provided on the upper surface of the apparatus main body 10.
  • the introduction means includes an introduction pipe 14 fixed to the upper wall portion of the apparatus main body 10 and for introducing the reduced volume gel-like polystyrene resin into the apparatus main body 10 from the outside;
  • the gutter-like member 16 is provided in the vicinity of the inner surface of the apparatus main body 10 in the circumferential direction, and the bottom surface 17 that defines the concave portion 15 is formed by, for example, a wire mesh of about 8 mesh.
  • the outer wall 18a is formed lower than the inner wall 18b. Also, this gutter-shaped part The material 16 is fixed to a stirring rod, which will be described later, via a supporting portion 19, and the gutter-shaped member 16 is also driven to rotate by rotating the stirring rod.
  • a heat medium flow pipe 20 is arranged in a spiral and vertically multilayered form along the inner surface of the apparatus main body. Both ends of the heat medium flow pipe 20 are drawn out to the outside from the side surface of the apparatus main body 10, and a heat medium such as, for example, heating oil or steam flows from one end of the heat medium flow pipe 20. 0 and is discharged to the outside from the other end. That is, the heat medium is always circulated in the heat medium flow pipe 20, and the surface of the heat medium flow pipe 20 is maintained at a predetermined temperature.
  • the heating oil is preferably introduced from the upper end. Introduced from the lower end.
  • a flow control member 21 for guiding the flow of the reduced volume gel-like polystyrene resin is provided along the heat medium flow tube 20 below the heat medium flow tube 20.
  • the flow control member 21 is basically composed of two control plates 22 and 23, and is arranged so that the interval between them becomes narrower toward the lower side.
  • the control plates are arranged such that the angle 0 between them is about 90 °.
  • the two control plates 22 and 23 are arranged such that the interval W at the lower end is smaller than the outer diameter D of the heat medium flow pipe 20.
  • the interval between the lower ends of the two control plates 22 and 23 is 3 Omm (FIG. 2). See).
  • the flow control member 21A provided below the lowermost heat medium flow pipe 20A is not a pair of control plates but a region corresponding to the lower side of the heat medium flow pipe 20A. It is composed of a hat-shaped member 24 having an inclined surface continuous to the vicinity of the side surface.
  • a heating means is continuously provided on the outer surface of the apparatus main body 10 in a region corresponding to the resin holding portion 13 from the heat medium flow pipe 2OA in the lowermost layer.
  • the heating means is not particularly limited as long as it can heat the wall surface of the apparatus main body 10.
  • a predetermined heat medium is circulated inside similarly to the heat medium flow pipe 20. Heat medium circulation means 25.
  • a stirring rod 27 having a projecting portion 26 provided in a spiral shape is provided in a region corresponding to the resin holding portion 13.
  • One end of the stirring rod 27 is connected to a drive motor 28 provided on the upper surface of the apparatus main body 10, and the other end is connected to a plurality of, for example, four legs on the bottom surface of the apparatus main body 10. It is rotatably held on a support 30 fixed by 29.
  • an end of the stirring rod 27 held on the support 30 is provided with a second stirring rod extending to the inside of the resin recovery section 12 connected to the E surface of the apparatus main body 10. 3 1 is connected. Then, when the stirring rod 27 rotates, the second stirring rod 31 also rotates at the same time.
  • the second stirring rod 31 also has a projection 32 similar to the stirring rod 27, and the second stirring rod 31 and the second stirring rod 31 rotate. The resin in the resin holding unit 13 is stirred while the resin in the resin holding unit 13 flows into the resin collecting unit 12.
  • a gutter-shaped member 16 is fixed to the upper portion of the stirring rod 27 via a support portion 19, and the gutter is rotated together with the rotation of the stirring rod 27 and the second stirring rod 31.
  • the shaped member 16 also rotates.
  • a heating medium circulation path 33 having a substantially cylindrical shape and through which a heating medium is circulated is provided. That is, the heat medium circulation path 33 is fixed on the support 30 on which the end of the stirring rod 27 is held. Although described in detail later, the heat medium circulation path 33 is provided for heating the resin held in the resin holding section 13.
  • a preheater 100 is connected to the introduction pipe 14 for introducing the reduced volume gel-like polystyrene resin.
  • the preheater 100 is, for example, a multi-stage heat exchanger, and is provided with a heat medium inlet 101 and a heat medium outlet 102 into which a heat medium such as steam flows.
  • the volume-reduced gel polystyrene resin introduced from the raw material inlet 104 is preheated, and the preheated volume-reduced gel polystyrene resin is discharged from the raw material outlet 104.
  • the volume-reduced gel polystyrene resin separation / recovery device of the present embodiment can efficiently separate and recover the volume-reduced gel polystyrene resin into a resin and a solvent.
  • the procedure for separating and recovering the reduced volume polystyrene resin will be described.
  • the volume-reduced gel polystyrene resin referred to here is a resin waste material such as polystyrene resin or foamed polystyrene whose apparent volume is larger than the actual volume of the resin component. Is contacted with a solvent to form a gel, the type of which is not particularly limited.
  • the bow I has a firing point of about 40 ° C. to 100 ° C., and the ignition point is 180 ° C. It is obtained by treating polystyrene resin or expanded polystyrene in a solvent at about ° C to 350 ° C.
  • volume-reduced gel polystyrene resin introduced into the preheater 100 is fluidized so that it flows to a certain degree, and if necessary, impurities such as dust are removed by filtration or the like. Is preferred.
  • a volume-reduced gel-like polystyrene resin is introduced into the inlet pipe 14 by preheating it to about 150 ° C. with a preheater 100 as necessary, for example, The low components are immediately vaporized in the decompressed apparatus body 10 and recovered from the solvent recovery section 11.
  • a low-boiling component in the solvent is removed immediately after introduction by preheating in a preheater 100.
  • the preheater 100 is not operated.
  • the preheater 100 is not always required to be provided, and a volume-reduced gel-like polystyrene resin in a fluidized state to some extent may be directly introduced into the introduction tube 14.
  • the volume-reduced gel polystyrene resin 50 when the volume-reduced gel polystyrene resin 50 is introduced into the apparatus main body 10 through the introduction tube 14, the volume-reduced gel polystyrene resin 50 becomes a stirring rod 27. Flows into the concave portion 15 of the gutter-like member 16 fixed to the bottom. At this time, since the gutter-like member 16 is rotationally driven together with the stirring rod 2.7, the concave part 15 of the gutter-like member 16 has a volume-reduced gel-like polystyrene resin 50 that is substantially uniformly distributed over the entire circumference. Flows in.
  • the volume-reduced gel-like polystyrene resin 50 overflows the concave portion 15 and flows through the heat medium. Runs down tube 20.
  • the volume-reduced gel-like polystyrene resin 50 overflowing from the recess 15 is formed from the outside of the gutter-shaped member 16 It flows along the outer surface of the shaped member 16 and flows down from its bottom surface onto the uppermost heat medium flow pipe 20.
  • the volume-reduced gel-like polystyrene resin 50 that has flowed down from the uppermost heat medium flow pipe 20 has its flow controlled by a flow control member 21 composed of two plate-like members 22, 23.
  • the heat medium flow pipe 20 on the lower layer side sequentially flows down.
  • a heating medium made of a heating oil is introduced into the inside of the heating medium circulation pipe 20, and the outer surface of the heating medium circulation pipe 20 is approximately 180 ° C. to 200 ° C. It is held in C. Therefore, the volume-reduced gel-like polystyrene resin 50 that has flowed down onto the heat medium flow pipe 20 is heated and removed by evaporating a part of the solvent.
  • the volume-reduced gel-like polystyrene resin 50 is repeatedly heated a plurality of times, and most of the solvent is removed. Is vaporized and removed. That is, by flowing down along the heat medium flow pipe 20, the volume-reduced gel polystyrene resin 50 becomes a resin from which the solvent has been substantially removed.
  • the vaporized solvent is discharged from the solvent recovery section 11 to the outside of the apparatus main body 10.
  • the vaporized solvent is removed from the solvent recovery section 11 are sequentially discharged from
  • the discharged solvent is liquefied by a condenser and collected in a collection tank.
  • the resin 60 from which the solvent has been removed by being heated a plurality of times by the heat medium flow pipe 20 and having flowed down from the lowermost heat medium flow pipe 2 OA has a flow control member 21 A It flows along the inner surface of the apparatus main body 10 via (24) and flows into the resin holder 13.
  • the heat medium circulation as the heating means is performed.
  • Means 25 are provided, and the wall surface of the apparatus main body 10 is maintained at, for example, about 230 ° C. Therefore, the flow from the flow control member 21 A to the wall of The resin 60 that has fallen is further heated to lower the viscosity and ensure fluidity, so that it flows into the resin holding portion 13 through the wall surface of the apparatus main body 10 well.
  • the resin 60 flowing into and held by the resin holding portion 13 is stirred by the projections 26 and 32 by rotating the stirring rod 27 and the second stirring rod 31. Further, the heat medium is sufficiently heated by the heat medium circulation means 25 and the heat medium circulation path 33. As a result, the solvent remaining in the resin 60 is completely vaporized and the air (bubbles) contained therein is also removed, and the resin 60 in the resin holding portion 13 has almost no solvent and bubbles. It will be completely removed.
  • the resin 60 held in the resin holding unit 13 is transferred to the resin recovery unit 12 by suction means (not shown) such as a gear pump for transferring molten plastic, for example. While continuously being guided by the protrusions 32 of the stirring rod 31, the resin continuously flows into the resin recovery unit 12.
  • suction means such as a gear pump for transferring molten plastic, for example.
  • the outer diameter of the protrusion 32 provided spirally on the second stirring rod 31 is formed to be substantially the same as the diameter of the opening of the resin recovery unit 12 on the apparatus main body 10 side. Therefore, the resin in the resin holding portion 12 flows into the resin collecting portion 12 by a constant amount at all times while being guided by the protrusion 32 by the rotation of the second stirring rod 31. Thereafter, the resin flowing into the resin recovery section 12 is sent to an extruder (not shown) by a delivery pump 40 and a drive motor 41 (see FIG. 1) provided therebelow to be formed into a rod-shaped member having a predetermined diameter. Is done. If a solvent or air bubbles remain in the resin, cracks or the like are likely to occur when the resin is formed into a rod-shaped member.
  • the solvent is removed by the volume-reduced gel-type polystyrene resin separation and recovery apparatus of the present invention.
  • the resin thus obtained is sufficiently heated in the resin holding section 13 and the solvent, bubbles, and the like are completely removed, so that cracks and the like do not occur during molding.
  • it is necessary to use an appropriate pump because bubbles may enter and enter depending on the type of the dispensing pump 40 for transferring the resin.
  • the volume-reduced gel-like polystyrene resin separation / recovery apparatus is used.
  • the apparatus body 10 is composed of a reduced volume gel-like polystyrene resin container 34 and a lid 35 (see FIG. 2).
  • the volume-reduced gel-like polystyrene resin container 34 and the lid 35 are fixed to each other by a fastening means such as a screw (not shown) with a flange 36. I Therefore, as shown in FIG. 5, the volume-reduced gel-like polystyrene resin container 34 and the lid 35 can be easily separated for maintenance. That is, at this time, there is a space between the stirring rod 27 and the heat medium flow pipe 20 provided around the stirring rod 27, etc., so that maintenance work is easy. Further, the lid 35 has a manhole portion 37, and at the top of the manhole portion 37, there is provided a viewing window 38 through which the inside can be seen.
  • FIG. 6 is a schematic diagram showing a main part of a volume-reduced gel-like polystyrene resin separation / recovery device according to Embodiment 2.
  • the resin recovery unit 12 connected to the lower part of the apparatus main body 10 is extended along the axial direction of the stirring rod 27 as a stirring means.
  • the transfer pipe 43 extends in a direction intersecting the axial direction of the stirring rod 27, for example, in a horizontal direction substantially orthogonal to the stirring rod 27 via the resin recovery section 12. Is the same as in the first embodiment.
  • a heating medium circulating means 44 as a heating means is provided.
  • the delivery pump 40 is connected to the pump connection part 45 at the end of the transfer pipe 43 as in the first embodiment.
  • the volume-reduced gel polystyrene resin separation and recovery apparatus of the present invention continuously and efficiently treats the volume-reduced gel polystyrene resin to separate the resin and the solvent, and recovers each. can do.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

The invention provides a volume-decreased gel-like polystyrene resin separating and recovering device wherein volume-decreased gel-like polystyrene resin is continuously and efficiently treated to separate and recover the solvent and resin. A separating and recovering device for separating and recovering the solvent and resin by heating volume-decreased gel-like polystyrene resin under ordinary pressure or reduced pressure, the device comprising a device main body (10) having in the upper region thereof a solvent recovering section for continuously recovering an evaporated solvent and in the lower region thereof a resin recovering section for recovering the solvent-removed resin, a heating medium flow pipe (20) disposed in the device main body (10) to allow the heating medium to flow therein, a gel resin introducing means (14) for introducing volume-decreased gel-like polystyrene resin in such a manner as to contact the heating medium flow pipe (20), a resin hold section (13) disposed in the lower region of the device main body (10) for holding the resin that contacts the heating medium flow pipe (20) and then flows downward, a heating means (25) for heating the resin held in this resin holding section (13), and an agitating means (26) for agitating the resin held in the resin holding section.

Description

明 細 書 減容化ゲル状ポリスチレン樹脂分離回収装置 技術分野  Description Volume-reduced gel polystyrene resin separation and recovery equipment Technical field
本発明は、 減容化ゲル状ポリスチレン樹脂から液体 (溶剤) 及び樹脂を回収 する技術に係り、 特に、 減容化ゲル状ポリスチレン樹脂から連続的に溶剤及び樹 脂を分離回収する減容化ゲル状ポリスチレン樹脂分離回収装置に関する。 背景技術  The present invention relates to a technique for recovering a liquid (solvent) and a resin from a volume-reduced gel polystyrene resin, and more particularly to a volume-reduced gel for continuously separating and recovering a solvent and a resin from a volume-reduced gel polystyrene resin. The present invention relates to an apparatus for separating and collecting a polystyrene resin. Background art
最近になって、 ポリスチレン樹脂や発泡ポリスチレンの樹脂廃材のように樹 脂成分の実容積よりも見かけの容積が大きい樹脂廃材の処理方法として樹脂廃材 を溶剤に接触させてゲル化させることによりその容積を実容積とほぼ同じ程度に 減少させ、 この後、 樹脂と溶剤とを分離し、 樹脂を燃料や樹脂原料として再利用 し、 又、 溶剤を同じ処理に再使用する技術が開発されている (特開平 2— 1 7 4 8号公報、 特開平 5— 5 9 2 1 2号公報、 特開平 7— 1 1 3 0 8 9号公報、 特開 平 9 ^ 4 0 8 0 2号公報、 特開平 9一 1 5 7 4 3 5号公報、 特開 2 0 0 1— 1 8 1 4 3 9号公報など参照) 。  Recently, as a method of treating resin waste materials such as polystyrene resin and foamed polystyrene resin waste materials that have an apparent volume larger than the actual volume of the resin component, the resin waste material is brought into contact with a solvent and gelled by contacting it with a solvent. A technology has been developed that reduces the resin to approximately the same volume as the actual volume, separates the resin from the solvent, reuses the resin as fuel and resin raw material, and reuses the solvent in the same process ( Japanese Unexamined Patent Application Publication Nos. Hei 2-174948, Hei 5-529212, Hei 7-113809, Hei 9 ^ 4082, (See, for example, Japanese Unexamined Patent Publication No. Hei 9-191, 734, 35 and Japanese Patent Application Laid-Open No. 2001-181,439)
この新規な技術分野において、 固形物である樹脂と液体である溶剤とを分離す る方法として、 溶剤を蒸発させて固形物と分離し、 その蒸気を凝縮させて回収す るという操作が提案されている。 すなわち、 一般的には、 樹脂廃材を溶剤に接触 させてその容積を樹脂の実容積とほぼ同じ程度に減少させる処理は減容ゲル化処 理、 或いは単に減容処理と呼ばれ、 餅のようになるまでゼリー状又はゲル状にゲ ル化された樹脂は減容化ゲル状ポリスチレン樹脂と言われている。 この減容化ゲ ル状ポリスチレン樹脂を樹脂と溶剤とに分離する方法としては、 減容化ゲル状ポ リスチレン樹脂の溶剤を蒸発させて分離する方法と、 減容化ゲル状ポリスチレン 榭脂を圧搾分離する方法とが提案されているが、 後の方法では樹脂中にわずかに 溶剤が残り、 必要に応じて、 この残りの溶剤を蒸発させることがある。  In this new technical field, as a method of separating a resin that is a solid from a solvent that is a liquid, an operation of evaporating the solvent to separate it from a solid, and condensing and collecting the vapor to recover the solvent has been proposed. ing. In other words, generally, the process of bringing resin waste material into contact with a solvent to reduce the volume to about the same as the actual volume of the resin is called a volume reduction gelling process or simply a volume reduction process. Resins that have been gelled in a jelly or gel form until they become are called reduced volume gel polystyrene resins. There are two methods of separating the volume-reduced gel polystyrene resin into a resin and a solvent: a method of evaporating the solvent of the volume-reduced gel polystyrene resin and a method of compressing the volume-reduced gel polystyrene resin. A separation method has been proposed, but in the latter method, a small amount of solvent remains in the resin, and the remaining solvent may be evaporated if necessary.
一般に、 液体 (溶剤) を蒸発させるには、 その液体 (溶剤) を加熱すればよく 、 蒸発させた液体 (溶剤) を回収するにはその蒸気を凝縮させて回収している。 また、 減容化ゲル状ポリスチレン樹脂や減容化ゲル状ポリスチレン樹脂から溶剤 を圧搾分離した樹脂から溶剤を蒸発させる場合にも、 加熱して溶剤を蒸発させて いる。 Generally, to evaporate a liquid (solvent), it is sufficient to heat the liquid (solvent). In order to recover the evaporated liquid (solvent), the vapor is condensed and recovered. In addition, when evaporating the solvent from the reduced volume gel polystyrene resin or the resin obtained by pressing and separating the solvent from the reduced volume gel polystyrene resin, the solvent is evaporated by heating.
例えば、 特開 2 0 0 1— 1 8 1 4 3 9号公報には、 ポリスチレンを溶剤に溶解 させてできたゲルに溶剤を加えて溶解液をつくる溶解槽と、 その溶解液を濾過す る濾過器と、 濾過器をでた溶解液から溶剤を蒸発させ所定の濃度の濃縮液をつく る濃縮器と、 その濃縮液から溶剤を蒸発分離しポリスチレンを取り出す分離器と を備えるポリスチレン回収装置が提案されている。 かかる装置の分離器は、 薄膜 蒸発式の分離器 9 0であり、 分離器内筒 9 1及び分離器外筒 9 2からなる二重構 造の容器からなり、 これら内筒 9 1と外筒 9 2の間に熱媒体を循環させて加熱す るものであり、 濃縮液は内筒 9 2に沿って導入される。 この場合、 導入された濃 縮液は溶剤が徐々に蒸発しながら内筒 9 2に沿って流下するが、 樹脂濃度が大き くなると流れ落ちなくなるので、 回転軸 9 5の周囲に複数の回転腕 9 6を介して 設けたかき取り板 9 7により内筒 9 2に付着した樹脂をかき取るようにしている しかしながら、 上述したような従来の、 樹脂と溶剤とを分離する分離器は、 一 般的には、 減容化ゲル状ポリスチレン樹脂を投入する装置本体を加熱しながら減 容化ゲル状ポリスチレン樹脂を流下させて溶剤を蒸発させるものであるが、 溶剤 の除去効率が低く、 また、 溶剤を十分に除去できず、 処理効率が十分ではないと いう問題がある。 さらに、 溶剤を除去した樹脂の品質も悪く、 樹脂を押し出して ペレツト化する場合には、 混入していた気泡により押し出される樹脂が途中で切 れてしまうなどの問題もある。 発明の開示  For example, Japanese Patent Application Laid-Open No. 2001-181439 discloses a dissolving tank for preparing a dissolving solution by adding a solvent to a gel obtained by dissolving polystyrene in a solvent, and filtering the dissolving solution. A polystyrene recovery device comprising a filter, a concentrator for evaporating the solvent from the solution passed through the filter to produce a concentrated solution having a predetermined concentration, and a separator for evaporating and separating the solvent from the concentrated solution to take out polystyrene. Proposed. The separator of such a device is a thin-film evaporation type separator 90, which is a double-structured container composed of a separator inner cylinder 91 and a separator outer cylinder 92. Heat is circulated between the heat exchangers 92 and heats the concentrate, and the concentrated liquid is introduced along the inner cylinder 92. In this case, the introduced concentrated liquid flows down along the inner cylinder 92 while the solvent gradually evaporates. However, when the resin concentration becomes high, the concentrated liquid does not flow down. However, the resin adhering to the inner cylinder 92 is scraped off by a scraping plate 97 provided via 6 However, the above-described conventional separator for separating the resin and the solvent is generally used. Is a method in which a volume-reduced gel polystyrene resin is poured while heating the main body of the device in which the volume-reduced gel polystyrene resin is injected to evaporate the solvent, but the solvent removal efficiency is low and the solvent is sufficiently However, there is a problem that the treatment efficiency is not sufficient. Furthermore, the quality of the resin from which the solvent has been removed is poor, and when the resin is extruded and pelletized, there is a problem in that the extruded resin is cut off along the way due to the air bubbles mixed in. Disclosure of the invention
本発明は、 このような事情に鑑み、 減容化ゲル状ポリスチレン樹脂を連続的に 且つ効率的に処理して溶剤及び樹脂を分離回収する減容化ゲル ポリスチレン榭 脂分離回収装置を提供することを課題とする。  The present invention has been made in view of the above circumstances, and provides a volume-reduced gel polystyrene resin separation and recovery apparatus for continuously and efficiently treating a volume-reduced gel polystyrene resin to separate and recover a solvent and a resin. As an issue.
上記課題を解決する本発明の第 1の態様は、 減容化ゲル状ポリスチレン樹脂を 常圧もしくは減圧下で加熱することにより溶剤と樹脂とを分離回収する分離回収 装置であって、 蒸発した溶剤を連続的に取り出す溶剤回収部を上部に有すると共 に溶剤が除去された樹脂を回収する樹脂回収部を下部に有する装置本体と、 この 装置本体内に配設されると共に内方に熱媒体を流通させる熱媒体流通管と、 この 熱媒体流通管に接触するように減容化ゲル状ポリスチレン樹脂を導入するゲル樹 脂導入手段と、 前記熱媒体流通管に接触して下方へ流れ落ちた樹脂を保持する前 記装置本体の下部に設けられた樹脂保持部と、 この樹脂保持部に保持される樹脂 を加熱する加熱手段と、 '前記樹脂保持部に保持される樹脂を攪拌する攪拌手段と を具備することを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置にある かかる第 1の態様では、 連続的に減容化ゲル状ポリスチレン樹脂を供袷しなが ら、 樹脂と溶剤とを分離すると共にそれぞれを回収することができ、 処理効率を 著しく向上することができる。 A first aspect of the present invention that solves the above-mentioned problem is that a reduced volume gel-like polystyrene resin A separation / recovery device that separates and recovers a solvent and a resin by heating under normal pressure or reduced pressure. An apparatus main body having a resin recovery section to be recovered at a lower portion, a heat medium flow pipe arranged in the apparatus main body and flowing a heat medium inward, and a volume reduced so as to contact the heat medium flow pipe. A gel resin introduction means for introducing a gel-like polystyrene resin, a resin holding portion provided at a lower portion of the apparatus main body for holding a resin that has flowed downward in contact with the heat medium flow pipe, and a resin holding portion provided with the resin holding portion. A heating means for heating the resin held in the resin holding section; and a stirring means for stirring the resin held in the resin holding section. In the first embodiment, while continuously supplying the volume-reduced gel-like polystyrene resin, the resin and the solvent can be separated and recovered, and the treatment efficiency can be significantly improved.
本発明の第 2の態様は、 第 1の態様において、 前記熱媒体流通管は、 前記装置 本体の周壁近傍に螺旋状に且つ上下方向に多層になるように配設されていること を特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置にある。  According to a second aspect of the present invention, in the first aspect, the heat medium flow pipe is spirally arranged near the peripheral wall of the apparatus main body so as to be multilayered in a vertical direction. In a volume-reduced gel-like polystyrene resin separation and recovery device.
かかる第 2の態様では、 減容化ゲル状ポリスチレン樹脂が熱媒体流通管に接触 することによつて加熱され、 減容化ゲル状ポリスチレン樹脂から溶剤が効率的に 分離'除去される。  In the second aspect, the volume-reduced gel-like polystyrene resin is heated by coming into contact with the heat medium flow tube, and the solvent is efficiently separated and removed from the volume-reduced gel-like polystyrene resin.
本発明の第 3の態様は、 第 1又は 2の態様において、 前記熱媒体流通管に接触 した減容化ゲル状ポリスチレン樹脂は、 当該熱媒体流通管に沿って流れると共に 上方に配置された熱媒体流通管から下方に配置された熱媒体流通管へ流れ落ちて 前記樹脂保持部へ移動することを特徴とする減容化ゲル状ポリスチレン樹脂分離 回収装置にある。  According to a third aspect of the present invention, in the first or second aspect, the volume-reduced gel-like polystyrene resin that has come into contact with the heat medium flow tube flows along the heat medium flow tube and is disposed above the heat medium flow tube. A volume-reduced gel-like polystyrene resin separation / recovery device characterized by flowing down from a medium flow tube to a heat medium flow tube arranged below and moving to the resin holding section.
かかる第 3の態様では、 減容化ゲル状ポリスチレン樹脂が熱媒体流通管に接触 している期間が長くなり、 減容化ゲル状ポリスチレン樹脂から溶媒を効率的且つ 確実に除去することができる。 '  In the third aspect, the period during which the volume-reduced gel-like polystyrene resin is in contact with the heat medium flow tube is lengthened, and the solvent can be efficiently and reliably removed from the volume-reduced gel-like polystyrene resin. '
本発明の第 4の態様は、 第 1〜3の何れかの態様において、 前記熱媒体流通管 の近傍には所定の間隔を開けて当該熱媒体流通管に接触して流れる前記減容化ゲ ル状ポリスチレン樹脂の流れを案内する流れ制御板が当該熱媒体流通管に沿って 設けられていることを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置に ある。 According to a fourth aspect of the present invention, in any one of the first to third aspects, the volume-reducing tube which flows in contact with the heat medium flow pipe at a predetermined interval in the vicinity of the heat medium flow pipe. A flow control plate for guiding the flow of the polystyrene resin is provided along the heat medium flow pipe.
かかる第 4の態様では、 熱媒体流通管から流れる減容化ゲル状ポリスチレン樹 脂が、 流れ制御板を介して、 その下側に配設されている熱媒体流通管上に確実に 接触する。  In the fourth aspect, the volume-reduced gel-like polystyrene resin flowing from the heat medium flow tube surely comes into contact with the heat medium flow tube disposed below the flow control plate via the flow control plate.
本発明の第 5の態様は、 第 4の態様において、 前記熱媒体流通管の一番下層の 下方の前記流れ制御板は、 当該熱媒体流通管から流れ落ちる樹脂を前記装置本体 の壁面方向へ案内するものであることを特徴とする減容化ゲル状ポリスチレン樹 脂分離回収装置にある。  In a fifth aspect of the present invention, in the fourth aspect, the flow control plate below the lowermost layer of the heat medium flow pipe guides the resin flowing down from the heat medium flow pipe toward the wall surface of the apparatus main body. A volume-reduced gel-like polystyrene resin separation / recovery apparatus characterized in that:
かかる第 5の態様では、 熱媒体流通管から流れ落ちる樹脂が、 加熱手段によつ て加熱された装置本体の壁面を介して樹脂保持部に流れ込むため、 樹脂が固化す ることなく流動性が確保される。  In the fifth aspect, the resin flowing down from the heat medium flow pipe flows into the resin holding portion via the wall surface of the apparatus main body heated by the heating means, so that the fluidity is secured without solidifying the resin. Is done.
本発明の第 6の態様は、 第 1〜 5の何れかの態様において、 前記加熱手段は、 前記装置本体の下部の壁面に沿って熱媒体を循環させる熱媒体循環手段を含むこ とを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置にある。  According to a sixth aspect of the present invention, in any one of the first to fifth aspects, the heating means includes a heat medium circulating means for circulating a heat medium along a lower wall surface of the apparatus main body. In a volume-reduced gel-like polystyrene resin separation and recovery device.
かかる第 6の態様では、 装置本体の壁面を流れる樹脂の流動性をより確実に保 持できる。  In the sixth aspect, the fluidity of the resin flowing on the wall surface of the apparatus main body can be more reliably maintained.
本発明の第 7の態様は、 第 1〜6の何れかの態様において、 前記加熱手段は、 前記樹脂保持部の略中央部底部に設けられた前記攪拌装置を囲むように設けられ た略円筒状の熱媒体循環路を含むことを特徴とする減容化ゲル状ポリスチレン樹 脂分離回収装置にある。  According to a seventh aspect of the present invention, in any one of the first to sixth aspects, the heating means is provided in a substantially cylindrical shape provided so as to surround the stirrer provided in a substantially central bottom of the resin holding part. A volume-reduced gel-like polystyrene resin separation / recovery device comprising a heat medium circulation path in a shape.
かかる第 7の態様では、 樹脂保持部内の樹脂が確実に加熱された所定温度に保 持され、 樹脂が固化するのを防止でき、 且つ樹脂内に残留している溶剤をほぼ完 全に除去できる。  In the seventh aspect, the resin in the resin holding portion is reliably maintained at the predetermined temperature at which the resin is heated, so that the resin can be prevented from solidifying, and the solvent remaining in the resin can be almost completely removed. .
本発明の第 8の態様は、 第 1〜 7の何れかの態様において、 前記ゲル樹脂導入 手段は、 前記熱媒体流通管の上方に配置されて回転駆動される樋状部材と、 該樋 状部材上に前記減容化ゲル状ポリスチレン樹脂を導入する導入流路とを具備し、 前記樋状部材から溢れた前記減容化ゲル状ポリスチレン樹脂が前記熱媒体流通管 上へ流れ落ちるようになつていることを特徴とする減容化ゲル状ポリスチレン樹 脂分離回収装置にある。 According to an eighth aspect of the present invention, in any one of the first to seventh aspects, the gel resin introducing means is disposed above the heat medium flow pipe and driven to rotate, and the gutter-shaped member is provided. An introduction flow path for introducing the volume-reduced gel polystyrene resin onto a member, wherein the volume-reduced gel polystyrene resin overflowing from the trough-like member is provided in the heat medium flow pipe. A volume-reduced gel-like polystyrene resin separation and recovery device characterized by flowing down.
力かる第 8の態様では、 装置本体の円周方向に亘つて、 減容化ゲル状ポリスチ レン樹脂が'略均等な量で樋状部材から熱媒体流通管上に流れ落ちる。  In the eighth mode, the volume-reduced gel-polystyrene resin flows down from the gutter-like member onto the heat medium flow pipe in a substantially uniform amount over the circumferential direction of the apparatus main body.
本発明の第 9の態様は、 第 1〜8の何れかの態様において、 前記樹脂回収部か ら下方に払い出された樹脂を略水平方向に移送する.移送管を具備し、 該移送管に 払い出しポンプを設けて樹脂を回収するようにしたことを特徴とする減容化ゲ 'ル 状ポリスチレン樹脂分離回収装置にある。  According to a ninth aspect of the present invention, in any one of the first to eighth aspects, the resin discharged from the resin recovery section is transferred in a substantially horizontal direction. And a pay-out pump is provided to collect the resin.
かかる第 9の態様では、 樹脂回収部から払い出された樹脂が払い出しポンプに 到達するために移送管を流れるので、 樹脂に含まれる気泡が著しく低減される。 本発明の第 1 0の態様は、 第 9の態様において、 前記移送管の周囲を加熱する 加熱手段を具備することを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装 置にある。 , かかる第 1 0の態様では、 移送管を流れる樹脂が加熱され、 その流動性が確保 される。 図面の簡単な説明  In the ninth aspect, the resin discharged from the resin recovery section flows through the transfer pipe to reach the discharge pump, so that bubbles contained in the resin are significantly reduced. According to a tenth aspect of the present invention, in the ninth aspect, there is provided an apparatus for separating and collecting a reduced volume gel-like polystyrene resin, comprising heating means for heating the periphery of the transfer tube. In the tenth aspect, the resin flowing through the transfer tube is heated, and its fluidity is ensured. BRIEF DESCRIPTION OF THE FIGURES
第 1図は、 本発明の実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離回収 装置の概略図である。  FIG. 1 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
第 2図は、 本発明の実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離回収 装置の要部の拡大図である。  FIG. 2 is an enlarged view of a main part of the volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
第 3図は、 本発明の実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離回収 装置を用いた分離回収手順を説明する概略図である。  FIG. 3 is a schematic diagram illustrating a separation and recovery procedure using a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
第 4図は、 本発明の実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離回収 装置を用いた分離回収手順を説明する概略図である。  FIG. 4 is a schematic diagram illustrating a separation and recovery procedure using a volume-reduced gel-like polystyrene resin separation and recovery apparatus according to Embodiment 1 of the present invention.
第 5図は、 本発明の実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離装置 の概略図である。  FIG. 5 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation device according to Embodiment 1 of the present invention.
第 6図は、 本発明の実施形態 2に係る減容化ゲル状ポリスチレン樹脂分離装置 の概略図である。 本発明を実施するための最良の形態 FIG. 6 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation device according to Embodiment 2 of the present invention. BEST MODE FOR CARRYING OUT THE INVENTION
以下、 本発明を各実施形態に基づいて詳細に説明する。  Hereinafter, the present invention will be described in detail based on embodiments.
(実施形態 1 )  (Embodiment 1)
第 1図は、 実施形態 1に係る減容化ゲル状ポリスチレン樹脂分離回収装置の概 略図であり、 第 2図は、 減容化ゲル状ポリスチレン樹脂分離回収装置の一部拡大 図である。  FIG. 1 is a schematic diagram of a volume-reduced gel-like polystyrene resin separation / recovery device according to Embodiment 1, and FIG. 2 is a partially enlarged view of the volume-reduced gel-like polystyrene resin separation / recovery device.
本実施形態の減容化ゲル状ポリスチレン樹脂分離回収装置は、 減容化ゲル状ポ リスチレン樹脂を減圧下で加熱することにより樹脂と溶剤とを分離しそれぞれ回 収するためのものであり、 略円筒形状を有する装置本体 1 0の上面に、 蒸発した 溶剤を連続的に取り出す溶剤回収部 1 1が設けられると共に、 装置本体 1 0の底 面に、 溶剤が除去された樹脂を回収するための樹脂回収部 1 2が設けられている 装置本体 1 0の下部は、 外径が上部よりも狭くなつており、 詳しくは後述する 1 減容化ゲル状ポリスチレン樹脂から溶剤が除去された樹脂が保持される樹脂 保持部 1 3となっている。 そして、 樹脂回収部 1 2は、 この樹脂保持部 1 3に接 続されている。  The volume-reduced gel-like polystyrene resin separation and recovery apparatus of the present embodiment is for separating a resin and a solvent by heating the volume-reduced gel-like polystyrene resin under reduced pressure, and recovering them, respectively. A solvent recovery unit 11 for continuously removing the evaporated solvent is provided on the upper surface of the cylindrical apparatus main body 10, and a resin for removing the solvent from which the solvent has been removed is provided on the bottom surface of the apparatus main body 10. The lower part of the device main body 10 where the resin recovery section 12 is provided has a smaller outer diameter than the upper part, and holds the resin from which the solvent has been removed from the volume-reduced gel-like polystyrene resin, which will be described in detail later. The resin holding portion 13 is formed. The resin collecting section 12 is connected to the resin holding section 13.
一方、 溶剤回収部 1 1には、 図示しないが、 凝縮器 (コンデンサ) や回収タン ク等に繋がる排気パイプが接続されている。 そして、 装置本体 1 0の内部はこの 排気パイプを介して常に吸引されて減圧状態となっている。  On the other hand, an exhaust pipe (not shown) connected to a condenser (condenser) and a recovery tank is connected to the solvent recovery section 11. Then, the inside of the apparatus main body 10 is constantly sucked through the exhaust pipe to be in a reduced pressure state.
また、 置本体 1 0の上面には、 減容化ゲル状ポリスチレン樹脂を装置本体 1 0內に導入するための導入手段が設けられている。 この導入手段は、 本実施形態 では、 装置本体 1 0の上壁部分に固定されて外部から装置本体 1 0内に減容化ゲ ル状ポリスチレン樹脂を導入するための導入管 1 4と、 装置本体 1 0内の上部に 配設され、 導入管 1 4を介して導入された減容化ゲル状ポリスチレン樹脂が一定 量貯留される凹部 1 5を有する樋状部材 1 6.とで構成されている。  In addition, an introduction means for introducing the volume-reduced gel-like polystyrene resin into the apparatus main body 10 is provided on the upper surface of the apparatus main body 10. In the present embodiment, the introduction means includes an introduction pipe 14 fixed to the upper wall portion of the apparatus main body 10 and for introducing the reduced volume gel-like polystyrene resin into the apparatus main body 10 from the outside; A gutter-like member 16 having a concave portion 15 disposed at an upper portion in the main body 10 and storing a fixed amount of the reduced volume gel-like polystyrene resin introduced through the introduction pipe 14. I have.
樋状部材 1 6は、 装置本体 1 0の内面近傍に円周方向に亘つて設けられ、 この 凹部 1 5を画成する底面 1 7は、 例えば、 8メッシュ程度の金網で形成され、 側 壁は外側壁 1 8 aが内側壁 1 8 bよりも低く形成されている。 また、 この樋状部 材 1 6は、 支持部 1 9を介して後述する撹拌棒に固定されており、 この撹拌棒が 回転駆動することによって樋状部材 1 6も回転駆動するようになっている。 The gutter-like member 16 is provided in the vicinity of the inner surface of the apparatus main body 10 in the circumferential direction, and the bottom surface 17 that defines the concave portion 15 is formed by, for example, a wire mesh of about 8 mesh. The outer wall 18a is formed lower than the inner wall 18b. Also, this gutter-shaped part The material 16 is fixed to a stirring rod, which will be described later, via a supporting portion 19, and the gutter-shaped member 16 is also driven to rotate by rotating the stirring rod.
この樋状部材 1 6の下方には、 熱媒体流通管 2 0が、 装置本体の内面に沿って 螺旋状且つ上下方向多層となるように配設されている。 この熱媒体流通管 2 0の 両端部は、 装置本体 1 0の側面から外部に引き出されており、 この一方の端部か ら、 例えば、 加熱オイル、 水蒸気等の熱媒体が熱媒体流通管 2 0の内部に導入さ れ、 他方の端部から外部に排出されるようになっている。 すなわち、 熱媒体流通 管 2 0内には常に熱媒体が循環されており、 熱媒体流通管 2 0の表面は所定の温 度に保持されている。 なお、 一般的には、 熱媒体として加熱オイルを用いる場合 には下側の端部から導入し、 水蒸気を用いる場合には上側の端部より導入するの が好ましく、 本実施形態では加熱オイルを下側の端部から導入している。  Below this gutter-like member 16, a heat medium flow pipe 20 is arranged in a spiral and vertically multilayered form along the inner surface of the apparatus main body. Both ends of the heat medium flow pipe 20 are drawn out to the outside from the side surface of the apparatus main body 10, and a heat medium such as, for example, heating oil or steam flows from one end of the heat medium flow pipe 20. 0 and is discharged to the outside from the other end. That is, the heat medium is always circulated in the heat medium flow pipe 20, and the surface of the heat medium flow pipe 20 is maintained at a predetermined temperature. In general, when heating oil is used as the heat medium, it is preferable to introduce the oil from the lower end, and when using steam, it is preferable to introduce the oil from the upper end. In the present embodiment, the heating oil is preferably introduced from the upper end. Introduced from the lower end.
また、 熱媒体流通管 2 0の下側には、 減容化ゲル状ポリスチレン樹脂の流れを 案内するための流れ制御部材 2 1が熱媒体流通管 2 0に沿って設けられている。 この流れ制御部材 2 1は、 基本的には二枚の制御板 2 2, 2 3からなり、 両者の 間隔が下側ほど狭くなるように配置されている。 本実施形態では、 両制御板のな す角 0が約 9 0 ° となるように配置した。 また、 二枚の制御板 2 2, 2 3は、 下 端の間隔 Wが、 熱媒体流通管 2 0の外径 Dよりも狭くなるように配置されている ことが好ましい。 例えば、 本実施形態では、 熱媒体流通管 2 0の外径が 4 0 mm であるのに対し、 二枚の制御板 2 2, 2 3の下端の間隔を 3 O mmとしている ( 第 2図参照) 。  A flow control member 21 for guiding the flow of the reduced volume gel-like polystyrene resin is provided along the heat medium flow tube 20 below the heat medium flow tube 20. The flow control member 21 is basically composed of two control plates 22 and 23, and is arranged so that the interval between them becomes narrower toward the lower side. In the present embodiment, the control plates are arranged such that the angle 0 between them is about 90 °. Further, it is preferable that the two control plates 22 and 23 are arranged such that the interval W at the lower end is smaller than the outer diameter D of the heat medium flow pipe 20. For example, in the present embodiment, while the outer diameter of the heat medium flow pipe 20 is 40 mm, the interval between the lower ends of the two control plates 22 and 23 is 3 Omm (FIG. 2). See).
最下層の熱媒体流通管 2 0 Aの下側に設けられる流れ制御部材 2 1 Aは、 二枚 の制御板ではなく、 熱媒体流通管 2 0 Aの下側に対応する領域から装置本体の側 面近傍まで連続する傾斜面を有する笠状部材 2 4からなる。  The flow control member 21A provided below the lowermost heat medium flow pipe 20A is not a pair of control plates but a region corresponding to the lower side of the heat medium flow pipe 20A. It is composed of a hat-shaped member 24 having an inclined surface continuous to the vicinity of the side surface.
また、 最下層の熱媒体流通管 2 O Aから樹脂保持部 1 3に対応する領域の装置 本体 1 0の外面には加熱手段が連続的に設けられている。 この加熱手段は、 装置 本体 1 0の壁面を加熱できるものであれば、 特に限定されないが、 本実施形態で は、 熱媒体流通管 2 0と同様に、 内部に所定の熱媒体が循環される熱媒体循環手 段 2 5である。  Further, a heating means is continuously provided on the outer surface of the apparatus main body 10 in a region corresponding to the resin holding portion 13 from the heat medium flow pipe 2OA in the lowermost layer. The heating means is not particularly limited as long as it can heat the wall surface of the apparatus main body 10. In the present embodiment, a predetermined heat medium is circulated inside similarly to the heat medium flow pipe 20. Heat medium circulation means 25.
樹脂保持部 1 3の中央部には、 樹脂保持部 1 3内の樹脂を撹拌するための撹拌 手段、 本実施形態では、 樹脂保持部 1 3に対応する領域に螺旋状に設けられた突 起部 2 6を有する撹拌棒 2 7が設けられている。 この撹拌棒 2 7は、 その一端が 装置本体 1 0の上面に設けられた駆動モータ 2 8に接続されると共に、 他端が、 装置本体 1 0の底面に複数本、 例えば 4本の脚部 2 9によって固定された支持台 3 0に回転可能に保持されている。 In the center of the resin holder 13, stirring is performed to stir the resin in the resin holder 13. Means In the present embodiment, a stirring rod 27 having a projecting portion 26 provided in a spiral shape is provided in a region corresponding to the resin holding portion 13. One end of the stirring rod 27 is connected to a drive motor 28 provided on the upper surface of the apparatus main body 10, and the other end is connected to a plurality of, for example, four legs on the bottom surface of the apparatus main body 10. It is rotatably held on a support 30 fixed by 29.
また、 本実施形態では、 支持台 3 0に保持されている撹拌棒 2 7の端部には、 装置本体 1 0の E面に接続された樹脂回収部 1 2内まで延びる第 2の撹拌棒 3 1 が接続されている。 そして、 撹拌棒 2 7が回転することにより第 2の撹拌棒 3 1 も同時に回転する。 また、 この第 2の撹拌棒 3 1にも、 撹拌棒 2 7と同様に突起 部 3 2が設けられており、 撹拌棒 2 7及び第 2の撹拌棒 3 1が回転することによ り、 樹脂保持部 1 3内の樹脂が撹拌されると共に、 樹脂保持部 1 3内の樹脂が樹 脂回収部 1 2に流れ込むようになっている。  In the present embodiment, an end of the stirring rod 27 held on the support 30 is provided with a second stirring rod extending to the inside of the resin recovery section 12 connected to the E surface of the apparatus main body 10. 3 1 is connected. Then, when the stirring rod 27 rotates, the second stirring rod 31 also rotates at the same time. The second stirring rod 31 also has a projection 32 similar to the stirring rod 27, and the second stirring rod 31 and the second stirring rod 31 rotate. The resin in the resin holding unit 13 is stirred while the resin in the resin holding unit 13 flows into the resin collecting unit 12.
なお、 上述したが、 撹拌棒 2 7の上部には、 支持部 1 9を介して樋状部材 1 6 が固定されており、 これら撹拌棒 2 7及び第 2の撹拌棒 3 1の回転と共に樋状部 材 1 6も回転するようになっている。  As described above, a gutter-shaped member 16 is fixed to the upper portion of the stirring rod 27 via a support portion 19, and the gutter is rotated together with the rotation of the stirring rod 27 and the second stirring rod 31. The shaped member 16 also rotates.
また、 この撹拌棒 2 7の周囲には、 略円筒形を有し内部に熱媒体が循環される 熱媒体循環路 3 3が設けられている。 すなわち、 熱媒体循環路 3 3は、 撹拌棒 2 7の端部が保持されている支持台 3 0上に固定されている。 なお、 この熱媒体循 環路 3 3は、 詳しくは後述するが、 樹脂保持部 1 3に保持されている樹脂を加熱 するために設けられている。  Around the stirring rod 27, a heating medium circulation path 33 having a substantially cylindrical shape and through which a heating medium is circulated is provided. That is, the heat medium circulation path 33 is fixed on the support 30 on which the end of the stirring rod 27 is held. Although described in detail later, the heat medium circulation path 33 is provided for heating the resin held in the resin holding section 13.
• なお、 本実施形態では、 減容化ゲル状ポリスチレン樹脂を導入するための導入 管 1 4には、 予熱器 1 0 0が接続されている。 予熱器 1 0 0は、 例えば、 多段式 の熱交換器であり、 水蒸気等の熱媒体が流入される熱媒体流入口 1 0 1及ぴ熱媒 体流出口 1 0 2が設けられており、 原料入口 1 0 3から導入された減容化ゲル状 ポリスチレン樹脂を予熱し、 予熱した減容化ゲル状ポリスチレン樹脂を原料出口 1 0 4から排出するようになっている。  • In this embodiment, a preheater 100 is connected to the introduction pipe 14 for introducing the reduced volume gel-like polystyrene resin. The preheater 100 is, for example, a multi-stage heat exchanger, and is provided with a heat medium inlet 101 and a heat medium outlet 102 into which a heat medium such as steam flows. The volume-reduced gel polystyrene resin introduced from the raw material inlet 104 is preheated, and the preheated volume-reduced gel polystyrene resin is discharged from the raw material outlet 104.
このような本実施形態の減容化ゲル状ポリスチレン樹脂分離回収装置では、 減 容化ゲル状ポリスチレン樹脂を樹脂と溶剤とに効率的に分離して回収することが できる。 以下、 本実施形態の減容化ゲル状ポリスチレン樹脂分離回収装置を用い た減容化ゲル状ポリスチレン樹脂の分離回収手順について説明する。 The volume-reduced gel polystyrene resin separation / recovery device of the present embodiment can efficiently separate and recover the volume-reduced gel polystyrene resin into a resin and a solvent. Hereinafter, using the volume-reduced gel-like polystyrene resin separation and recovery apparatus of the present embodiment The procedure for separating and recovering the reduced volume polystyrene resin will be described.
なお、 ここで言う減容化ゲル状ポリスチレン樹脂とは、 ポリスチレン樹脂や発 泡ポリスチレンなどの樹脂廃材のように樹脂成分の実容積よりも見かけの容積が 大きレ、樹脂廃材の処理方法として樹脂廃材を溶剤に接触させてゲル化させたもの であり、 その種類は特に限定されないが、 本実施形態では、 弓 I火点が 4 0 °C〜1 0 0 °C程度、 発火点が 1 8 0 °C〜3 5 0 °C程度の溶剤にポリスチレン樹脂や発泡 ポリスチレンを処理したものである。  The volume-reduced gel polystyrene resin referred to here is a resin waste material such as polystyrene resin or foamed polystyrene whose apparent volume is larger than the actual volume of the resin component. Is contacted with a solvent to form a gel, the type of which is not particularly limited. In the present embodiment, the bow I has a firing point of about 40 ° C. to 100 ° C., and the ignition point is 180 ° C. It is obtained by treating polystyrene resin or expanded polystyrene in a solvent at about ° C to 350 ° C.
ここで、 予熱器 1 0 0に導入される減容化ゲル状ポリスチレン樹脂は、 ある程 度流動するように流動化させ、 必要に応じて濾過等によりゴミ等の不純物を除去 したものとするのが好ましい。 また、 このような減容化ゲル状ポリスチレン樹脂 は、 必要に応じて予熱器 1 0 0で、 例えば、 1 5 0 °C程度に予熱して導入管 1 4 に導入するようにすると、 沸点の低い成分は減圧状態となった装置本体 1 0内で 直ぐに気化し、 溶媒回収部 1 1から回収されるようになる。  Here, it is assumed that the volume-reduced gel polystyrene resin introduced into the preheater 100 is fluidized so that it flows to a certain degree, and if necessary, impurities such as dust are removed by filtration or the like. Is preferred. In addition, if such a volume-reduced gel-like polystyrene resin is introduced into the inlet pipe 14 by preheating it to about 150 ° C. with a preheater 100 as necessary, for example, The low components are immediately vaporized in the decompressed apparatus body 10 and recovered from the solvent recovery section 11.
なお、 本実施形態では、 ¾火点が装置本体 1 0内の温度より低い溶剤を処理す る場合には、 予熱器 1 0 0で予熱して溶剤中の低沸点成分が導入後直ぐに除去さ れるようにし、 発火点が比較的高い溶剤を処理する場合には、 予熱器 1 0 0を作 動させないようにしている。 なお、 予熱器 1 0 0は必ずしも設ける必要はなく、 ある程度流動する状態とした減容化ゲル状ポリスチレン樹脂を直接導入管 1 4に 導入するようにしてもよい。  In the present embodiment, when a solvent having a lower flash point than the temperature in the apparatus main body 100 is to be treated, a low-boiling component in the solvent is removed immediately after introduction by preheating in a preheater 100. In the case of processing a solvent having a relatively high ignition point, the preheater 100 is not operated. The preheater 100 is not always required to be provided, and a volume-reduced gel-like polystyrene resin in a fluidized state to some extent may be directly introduced into the introduction tube 14.
第 3図に示すように、 導入管 1 4を介して減容化ゲル状ポリスチレン樹脂 5 0 装置本体 1 0内に導入されると、 減容化ゲル状ポリスチレン樹脂 5 0は、 撹拌 棒 2 7に固定された樋状部材 1 6の凹部 1 5に流れ込む。 このとき、 樋状部材 1 6は、 撹拌棒 2.7と共に回転駆動されているため、 樋状部材 1 6の凹部 1 5には 、 全周に亘つて略均等に減容化ゲル状ポリスチレン樹脂 5 0が流れ込む。  As shown in FIG. 3, when the volume-reduced gel polystyrene resin 50 is introduced into the apparatus main body 10 through the introduction tube 14, the volume-reduced gel polystyrene resin 50 becomes a stirring rod 27. Flows into the concave portion 15 of the gutter-like member 16 fixed to the bottom. At this time, since the gutter-like member 16 is rotationally driven together with the stirring rod 2.7, the concave part 15 of the gutter-like member 16 has a volume-reduced gel-like polystyrene resin 50 that is substantially uniformly distributed over the entire circumference. Flows in.
そして、 凹部 1 5に流れ込んだ減容化ゲル状ポリスチレン樹脂 5 0は底面 1. 7 を形成する金網上を流れながら一部が減速されつつ当該金網を通過して下方の熱 媒体流通管 2 0上に流れ落ち、 当該凹部 1 5上に一定量の減容化ゲル状ポリスチ レン樹脂 5 0が貯留されると、 減容化ゲル状ポリスチレン樹脂 5 0は、 この凹部 1 5を溢れて熱媒体流通管 2 0上に流れ落ちる。 すなわち、 上述したように凹部 1 5の外側壁 1 8 aは内側壁 1 8 bよりも低く形成されているため、 凹部 1 5か ら溢れた減容化ゲル状ポリスチレン樹脂 5 0は、 樋状部材 1 6の外側から樋状部 材 1 6の外面を伝って流れ出し、 その底面から最上層の熱媒体流通管 2 0上に流 れ落ちる。 The volume-reduced gel-like polystyrene resin 50 that has flowed into the concave portion 15 flows through the wire mesh forming the bottom surface 1.7 while being partially decelerated, passes through the wire mesh, and passes through the lower heat medium flow pipe 20. When a certain amount of reduced volume gel-like polystyrene resin 50 is stored on the concave portion 15, the volume-reduced gel-like polystyrene resin 50 overflows the concave portion 15 and flows through the heat medium. Runs down tube 20. That is, as described above, Since the outer wall 18a of 15 is formed lower than the inner wall 18b, the volume-reduced gel-like polystyrene resin 50 overflowing from the recess 15 is formed from the outside of the gutter-shaped member 16 It flows along the outer surface of the shaped member 16 and flows down from its bottom surface onto the uppermost heat medium flow pipe 20.
また、 最上層の熱媒体流通管 2 0から流れ落ちた減容化ゲル状.ポリスチレン樹 脂 5 0は、 二枚の板状部材 2 2, 2 3からなる流れ制御部材 2 1によって流れが 制御され、 下層側の熱媒体流通管 2 0上に順次流れ落ちるようになつている。 ここで、 熱媒体流通管 2 0の内部には、 本実施形態では、 加熱オイルからなる 熱媒体が導入され、 熱媒体流通管 2 0の外面は、 約 1 8 0 °C〜2 0 0 °Cに保持さ れている。 したがって、 熱媒体流通管 2 0上に流れ落ちた減容化ゲル状ポリスチ レン樹脂 5 0は加熱され、 溶剤の一部が気化されることによって除去される。 そ して、 本実施形態では、 熱媒体流通管 2 0が多層となるように配設されているた め、 減容化ゲル状ポリスチレン樹脂 5 0は、 複数回繰り返し加熱され、 溶剤の大 部分が気化されて除去される。 すなわち、 熱媒体流通管 2 0に沿って流れ落ちる ことにより、 減容化ゲル状ポリスチレン樹脂 5 0は、 溶剤が実質的に除去された 樹脂となる。  In addition, the volume-reduced gel-like polystyrene resin 50 that has flowed down from the uppermost heat medium flow pipe 20 has its flow controlled by a flow control member 21 composed of two plate-like members 22, 23. The heat medium flow pipe 20 on the lower layer side sequentially flows down. Here, in the present embodiment, a heating medium made of a heating oil is introduced into the inside of the heating medium circulation pipe 20, and the outer surface of the heating medium circulation pipe 20 is approximately 180 ° C. to 200 ° C. It is held in C. Therefore, the volume-reduced gel-like polystyrene resin 50 that has flowed down onto the heat medium flow pipe 20 is heated and removed by evaporating a part of the solvent. In the present embodiment, since the heat medium flow tubes 20 are arranged in a multilayer structure, the volume-reduced gel-like polystyrene resin 50 is repeatedly heated a plurality of times, and most of the solvent is removed. Is vaporized and removed. That is, by flowing down along the heat medium flow pipe 20, the volume-reduced gel polystyrene resin 50 becomes a resin from which the solvent has been substantially removed.
—方、 気化された溶剤は、 溶剤回収部 1 1から装置本体 1 0の外部に排出され る。 上述したように、 装置本体 1 0内は、 溶剤回収部 1 1に接続された排気パイ プを介して吸引されて常に減圧状態となっているため、 気化された溶剤は溶剤回 収部 1 1から逐次排出される。 なお、 排出された溶剤は、 図示しないが、 凝縮器 (コンデンサ) によって液化されて回収タンクに回収される。  On the other hand, the vaporized solvent is discharged from the solvent recovery section 11 to the outside of the apparatus main body 10. As described above, since the inside of the apparatus main body 10 is constantly depressurized by being sucked through the exhaust pipe connected to the solvent recovery section 11, the vaporized solvent is removed from the solvent recovery section 11 Are sequentially discharged from Although not shown, the discharged solvent is liquefied by a condenser and collected in a collection tank.
そして、 第 4図に示すように、 熱媒体流通管 2 0によって複数回加熱され溶剤 が除去された樹脂 6 0は、 最下層の熱媒体流通管 2 O Aから流れ落ちると、 流れ 制御部材 2 1 A ( 2 4 ) を介して装置本体 1 0の内面を伝って樹脂保持部 1 3に 流れ込む。  Then, as shown in FIG. 4, the resin 60 from which the solvent has been removed by being heated a plurality of times by the heat medium flow pipe 20 and having flowed down from the lowermost heat medium flow pipe 2 OA, has a flow control member 21 A It flows along the inner surface of the apparatus main body 10 via (24) and flows into the resin holder 13.
ここで、 装置本体 1 0の下部、 すなわち、 流れ制御部材 2 1 A ( 2 4 ) 近傍か ら樹脂保持部 1 3に対応する領域に亘つて、 上述したように加熱手段である熱媒 体循環手段 2 5が設けられ、 装置本体 1 0の壁面は、 例えば、 約 2 3 0 °C程度に 保持されている。 したがって、 流れ制御部材 2 1 Aから装置本体 1 0の壁面に流 れ落ちた樹脂 6 0は、 さらに加熱されて粘度が低くなり流動性が確保されるため 、 装置本体 1 0の壁面を介して樹脂保持部 1 3内に良好に流れ込む。 Here, from the lower part of the apparatus main body 10, that is, from the vicinity of the flow control member 21 A (24) to the region corresponding to the resin holding part 13, as described above, the heat medium circulation as the heating means is performed. Means 25 are provided, and the wall surface of the apparatus main body 10 is maintained at, for example, about 230 ° C. Therefore, the flow from the flow control member 21 A to the wall of The resin 60 that has fallen is further heated to lower the viscosity and ensure fluidity, so that it flows into the resin holding portion 13 through the wall surface of the apparatus main body 10 well.
そして、 樹脂保持部 1 3に流れ込んで保持された樹脂 6 0は、 撹拌棒 2 7及び 第 2の撹拌棒 3 1が回転されることにより、 各突起部 2 6, 3 2によって撹拌さ れる。 また、 '熱媒体循環手段 2 5及び熱媒体循環路 3 3によって十分に加熱され る。 これにより、 樹脂 6 0の内部に残留している溶剤が完全に気化すると共に含 有される空気 (気泡) も除去され、 樹脂保持部 1 3内の樹脂 6 0は、 溶剤及び気 泡がほぼ完全に除去された状態となる。  Then, the resin 60 flowing into and held by the resin holding portion 13 is stirred by the projections 26 and 32 by rotating the stirring rod 27 and the second stirring rod 31. Further, the heat medium is sufficiently heated by the heat medium circulation means 25 and the heat medium circulation path 33. As a result, the solvent remaining in the resin 60 is completely vaporized and the air (bubbles) contained therein is also removed, and the resin 60 in the resin holding portion 13 has almost no solvent and bubbles. It will be completely removed.
樹脂保持部 1 3内に保持されている樹脂 6 0は、 樹脂回収部 1 2に接続された 、 例えば、 溶融プラスチック移送用ギヤポンプ等の吸引手段 (図示なし) によつ て移送され、 第 2の撹拌棒 3 1の突起部 3 2によってガイ ドされながら、 連続的 に樹脂回収部 1 2に流れ込む。  The resin 60 held in the resin holding unit 13 is transferred to the resin recovery unit 12 by suction means (not shown) such as a gear pump for transferring molten plastic, for example. While continuously being guided by the protrusions 32 of the stirring rod 31, the resin continuously flows into the resin recovery unit 12.
すなわち、 第 2の撹拌棒 3 1に螺旋状に設けられている突起部 3 2の外径は、 樹脂回収部 1 2の装置本体 1 0側の開口の直径と略同一の直径で形成されている ため、 樹脂保持部 1 2内の樹脂は、 第 2の撹拌棒 3 1が回転すること,により、 突 起部 3 2にガイドされながら常に一定の量ずつ樹脂回収部 1 2に流れ込む。 その後、 樹脂回収部 1 2に流れ込んだ樹脂は、 この下に設けられた払い出しポ ンプ 4 0及び駆動モータ 4 1 (第 1図参照) によって図示しない押し出し装置に 送られ所定径の棒状部材に成形される。 なお、 樹脂に溶剤又は気泡等が残留して いると、 樹脂を棒状部材に成形する際に割れ等が発生しやすいが、 本発明の減容 化ゲル状ポリスチレン樹脂分離回収装置では、 溶剤を除去した樹脂が、 樹脂保持 部 1 3で十分に加熱され、 溶剤あるいは気泡等が完全に除去されているため、 成 形時に割れ等が発生することがない。 また、 樹脂の移送用の払い出しポンプ 4 0 の種類により気泡が入,り込むこともあるので、 適正なポンプを用いる必要がある なお、 本実施形態の減容化ゲル状ポリスチレン樹脂分離回収装置では、 装置本 体 1 0が、 減容化ゲル状ポリスチレン樹脂収容体 3 4と蓋体 3 5とからなる (第 2図参照) 。 また、 これら減容化ゲル状ポリスチレン樹脂収容体 3 4と蓋体 3 5 とはフランジ 3 6でねじ等の締結手段 (図示なし) によって固定されている。 し たがって、 第 5図に示すように、 減容化ゲル状ポリスチレン樹脂収容体 3 4と蓋 体 3 5とを容易に分離してメンテナンスを行うことができる。 すなわち、 このと き、 攪拌棒 2 7とその周囲に設けられた熱媒体流通管 2 0等との間には、 作業者 が入るだけの空間があるので、 メンテナンス作業が容易である。 さらに、 蓋体 3 5にはマンホール部 3 7を有し、 マンホール部 3 7の頂点には、 内部を靦くこと ができる視き窓 3 8が設けられている。 That is, the outer diameter of the protrusion 32 provided spirally on the second stirring rod 31 is formed to be substantially the same as the diameter of the opening of the resin recovery unit 12 on the apparatus main body 10 side. Therefore, the resin in the resin holding portion 12 flows into the resin collecting portion 12 by a constant amount at all times while being guided by the protrusion 32 by the rotation of the second stirring rod 31. Thereafter, the resin flowing into the resin recovery section 12 is sent to an extruder (not shown) by a delivery pump 40 and a drive motor 41 (see FIG. 1) provided therebelow to be formed into a rod-shaped member having a predetermined diameter. Is done. If a solvent or air bubbles remain in the resin, cracks or the like are likely to occur when the resin is formed into a rod-shaped member. However, the solvent is removed by the volume-reduced gel-type polystyrene resin separation and recovery apparatus of the present invention. The resin thus obtained is sufficiently heated in the resin holding section 13 and the solvent, bubbles, and the like are completely removed, so that cracks and the like do not occur during molding. In addition, it is necessary to use an appropriate pump because bubbles may enter and enter depending on the type of the dispensing pump 40 for transferring the resin.In the present embodiment, the volume-reduced gel-like polystyrene resin separation / recovery apparatus is used. The apparatus body 10 is composed of a reduced volume gel-like polystyrene resin container 34 and a lid 35 (see FIG. 2). The volume-reduced gel-like polystyrene resin container 34 and the lid 35 are fixed to each other by a fastening means such as a screw (not shown) with a flange 36. I Therefore, as shown in FIG. 5, the volume-reduced gel-like polystyrene resin container 34 and the lid 35 can be easily separated for maintenance. That is, at this time, there is a space between the stirring rod 27 and the heat medium flow pipe 20 provided around the stirring rod 27, etc., so that maintenance work is easy. Further, the lid 35 has a manhole portion 37, and at the top of the manhole portion 37, there is provided a viewing window 38 through which the inside can be seen.
(実施形態 2 )  (Embodiment 2)
第 6図は、 実施形態 2に係る減容化ゲル状ポリスチレン樹脂分離回収装置の要 部,を示す概略図である。  FIG. 6 is a schematic diagram showing a main part of a volume-reduced gel-like polystyrene resin separation / recovery device according to Embodiment 2.
実施形態 1では、 装置本体 1 0の下部に接続される樹脂回収部 1 2が、 撹拌手 段である撹拌棒 2 7の軸方向に沿って延設されていたのに対し、 本実施形態では 、 第 6図に示すように、 樹脂回収部 1 2を介して、 撹拌棒 2 7の軸方向に交差す る方向、 例えば、 略直交する水平方向に移送管 4 3が延設されている以外は、 実 施形態 1と同様である。 また、 移送管 4 3の周囲には加熱手段である熱媒体循環 手段 4 4が設けられている。 勿論、 移送管 4 3の端部のポンプ接続部 4 5には払 い出しポンプ 4 0が接続されている点は実施形態 1と同様である。  In the first embodiment, the resin recovery unit 12 connected to the lower part of the apparatus main body 10 is extended along the axial direction of the stirring rod 27 as a stirring means. As shown in FIG. 6, the transfer pipe 43 extends in a direction intersecting the axial direction of the stirring rod 27, for example, in a horizontal direction substantially orthogonal to the stirring rod 27 via the resin recovery section 12. Is the same as in the first embodiment. Around the transfer pipe 43, a heating medium circulating means 44 as a heating means is provided. Needless to say, the delivery pump 40 is connected to the pump connection part 45 at the end of the transfer pipe 43 as in the first embodiment.
このような構成では、 第 2の攪拌棒 3 1の突起部 3 2による攪拌部と払い出し ポンプ 4 0とを移送管 4 3の分だけ隔離できるためか.、 払い出される樹脂内の気 泡の量がさらに著しく低減し、 押し出し成形時の不良率が著しく低減した。 なお、 このように移送管 4 3を設けると、 複数の減容化ゲル状ポリスチレン樹 脂分離回収装置からの移送管 4 3をポンプ接続部 4 5.に接続し、 一台の払い出し ポンプ 4 0で複数の減容化ゲル状ポリスチレン樹脂分離回収装置から樹脂を払い 出すことができるという利点もある。 産業上の利用可能性  In such a configuration, because the stirring section formed by the projections 32 of the second stirring rod 31 and the dispensing pump 40 can be separated by the transfer pipe 43, the amount of bubbles in the dispensed resin And the rejection rate during extrusion was significantly reduced. When the transfer pipes 43 are provided in this way, the transfer pipes 43 from a plurality of volume-reduced gel-like polystyrene resin separation / recovery devices are connected to the pump connection part 45, and one delivery pump 40 is provided. Another advantage is that the resin can be discharged from a plurality of volume-reduced gel-like polystyrene resin separation and recovery devices. Industrial applicability
以上説明したように、 本発明の減容化ゲル状ポリスチレン樹脂分離回収装置で は、 減容化ゲル状ポリスチレン樹脂を連続的且つ効率的に処理して樹脂と溶剤と を分離し、 それぞれを回収することができる。  As described above, the volume-reduced gel polystyrene resin separation and recovery apparatus of the present invention continuously and efficiently treats the volume-reduced gel polystyrene resin to separate the resin and the solvent, and recovers each. can do.

Claims

請 求 の 範 囲 The scope of the claims
1 . 減容化ゲル状ポリスチレン樹脂を常圧もしくは減圧下で加熱することに より溶剤と樹脂とを分離回収する分離回収装置であって、 蒸発した溶剤を連続的 に取り出す溶剤回収部を上部に有すると共に溶剤が除去された樹脂を回収する樹 脂回収部を下部に有する装置本体と、 この装置本体内に配設されると共に内方に 熱媒体を流通させる熱媒体流通管と、 この熱媒体流通管に接触するように減容化 ゲル状ポリスチレン樹脂を導入するゲル樹脂導入手段と、 前記熱媒体流通管に接 触して下方へ流れ落ちた樹脂を保持する前記装置本体の下部に設けられた樹脂保 持部と、 この樹脂保持部に保持される樹脂を加熱する加熱手段と、.前記樹脂保持 部に保持される樹脂を攪拌する攪拌手段とを具備することを特徴とする減容化ゲ ル状ポリスチレン樹脂分離回収装置。 1. Separation and recovery equipment that separates and recovers solvent and resin by heating volume-reduced gel polystyrene resin under normal pressure or reduced pressure, and has a solvent recovery section at the top to continuously remove evaporated solvent. An apparatus main body having a resin collecting section at the bottom for recovering the resin from which the solvent has been removed, a heat medium flow pipe disposed in the apparatus main body and for flowing a heat medium inward, and a heat medium A gel resin introduction means for introducing a gel-like polystyrene resin so as to be in contact with the flow pipe; and a gel resin introduction means provided at a lower portion of the apparatus main body for holding the resin that has flowed downward in contact with the heat medium flow pipe. A resin holding section; heating means for heating the resin held in the resin holding section; and stirring means for stirring the resin held in the resin holding section. Ru-shaped polystyrene Resin separation and recovery equipment.
2 . 特許請求の範囲 1において、 前記熱媒体流通管は、 前記装置本体の周壁 近傍に螺旋状に且つ上下方向に多層になるように配設されていることを特徴とす る減容化ゲル状ポリスチレン樹脂分離回収装置。 2. The volume-reducing gel according to claim 1, wherein the heat medium flow pipe is spirally disposed in the vicinity of a peripheral wall of the apparatus main body so as to be multilayered in a vertical direction. -Like polystyrene resin separation and recovery equipment.
3 . 特許請求の範囲 1又は 2において、 前記熱媒体流通管に接触した減容化 ゲル状ポリスチレン樹脂は、 当該熱媒体流通管に沿って流れると共に上方に配置 された熱媒体流通管から下方に配置された熱媒体流通管へ流れ落ちて前記樹脂保 持部へ移動することを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置。 3. In claim 1 or 2, the volume-reduced gel-like polystyrene resin that has come into contact with the heat medium flow tube flows downward along the heat medium flow tube arranged along the heat medium flow tube. A volume-reduced gel-like polystyrene resin separation / recovery device characterized by flowing down to a heat medium flow pipe arranged and moving to the resin holding section.
4 . 特許請求の範囲 1〜 3の何れかにおいて、 前記熱媒体流通管の近傍には 所定の間隔を開けて当該熱媒体流通管に接触して流れる前記減容化ゲル状ポリス チレン榭脂の流れを案内する流れ制御板が当該熱媒体流通管に沿って設けられて いることを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置。 4. In any one of claims 1 to 3, the volume-reduced gel-like polystyrene resin flowing in contact with the heat medium flow pipe at a predetermined interval in the vicinity of the heat medium flow pipe. A volume-reduced gel-like polystyrene resin separation / recovery device, wherein a flow control plate for guiding a flow is provided along the heat medium flow tube.
5 . 特許請求の範囲 4において、 前記熱媒体流通管の一番下層の下方の前記 流れ制御板は、 当該熱媒体流通管から流れ落ちる樹脂を前記装置本体の壁面方向 へ案内するものであることを特徴とする減容化ゲル状ポリスチレン樹脂分離回収 5. In Claim 4, the flow control plate below the lowermost layer of the heat medium flow pipe is configured to move resin flowing down from the heat medium flow pipe toward a wall surface of the apparatus main body. Volume-reduced gel polystyrene resin separation and recovery
6 . 特許請求の範囲 1〜5の何れかにおいて、 前記加熱手段は、 前記装置本 体の下部の壁面に沿って熱媒体を循環させる熱媒体循環手段を含むことを特徴と する減容化ゲル状ポリスチレン樹脂分離回収装置。 6. The volume-reducing gel according to any one of claims 1 to 5, wherein the heating means includes a heat medium circulating means for circulating a heat medium along a lower wall surface of the device body. -Like polystyrene resin separation and recovery equipment.
7 . 特許請求の範囲 1〜6の何れかにおいて、 前記加熱手段は、 前記樹脂保 持部の略中央部底部に設けられた前記攪拌装置を囲むように設けられた略円筒状 の熱媒体循環路を含むことを特徴とする減容化ゲル状ポリスチレン樹脂分離回収 7. The heating medium according to any one of claims 1 to 6, wherein the heating means is a substantially cylindrical heat medium circulation provided so as to surround the stirring device provided at a substantially central bottom of the resin holding part. Separation and recovery of reduced volume gel-like polystyrene resin characterized by including a channel
8 . 特許請求の範囲 1〜 7の何れかにおいて、 前記ゲル樹脂導入手段は、 前 記熱媒体流通管の上方に配置されて回転駆動される樋状部材と、 該樋状部材上に 前記減容化ゲル状ポリスチレン樹脂を導入する導入流路とを具備し、 前記樋状部 材から溢れた前記減容化ゲル状ポリスチレン樹脂が前記熱媒体流通管上へ流れ落 ちるようになつていることを特徴とする減容化ゲル状ポリスチレン樹脂分離回収 8. In any one of claims 1 to 7, wherein the gel resin introduction means is disposed above the heat medium flow pipe and is driven to rotate, and the gutter-like member is provided on the gutter-like member. An introduction flow path for introducing a volume-condensed gel polystyrene resin, wherein the volume-reduced gel polystyrene resin overflowing from the trough-shaped member flows down onto the heat medium flow tube. Separation and recovery of reduced volume gel-like polystyrene resin characterized by
9 . 特許請求の範囲 1〜8の何れかにおいて、 前記樹脂回収部から下方に払 い出された樹脂を略水平方向に移送する移送管を具備し、 該移送管に払い出しポ ンプを設けて樹脂を回収するようにしたことを特徴とする減容化ゲル状ポリスチ レン樹脂分離回収装置。 9. The transfer pipe according to any one of claims 1 to 8, further comprising a transfer pipe for transferring the resin discharged from the resin recovery section downward in a substantially horizontal direction, and a discharge pump provided in the transfer pipe. A volume-reduced gel-like polystyrene resin separation and recovery device characterized in that the resin is recovered.
1 0 . 特許請求の範囲 9において、 前記移送管の周囲を加熱する加熱手段を 具備することを特徴とする減容化ゲル状ポリスチレン樹脂分離回収装置。 10. The apparatus for separating and collecting a volume-reduced gel-like polystyrene resin according to claim 9, further comprising heating means for heating the periphery of the transfer tube.
11正された用紙 (規則 91) 11 Corrected forms (Rule 91)
PCT/JP2002/010098 2002-09-27 2002-09-27 Volume-decreased gel-like polystyrene resin separating and recovering device WO2004029140A1 (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
PCT/JP2002/010098 WO2004029140A1 (en) 2002-09-27 2002-09-27 Volume-decreased gel-like polystyrene resin separating and recovering device
AU2002332344A AU2002332344A1 (en) 2002-09-27 2002-09-27 Volume-decreased gel-like polystyrene resin separating and recovering device
US10/529,482 US7666368B2 (en) 2002-09-27 2003-09-26 Apparatus for treating volume-reduced polystyrene resin in gel state for material separation and recovery
AU2003268682A AU2003268682A1 (en) 2002-09-27 2003-09-26 Apparatus for the separation and recovery of volume-reduced polystyrene resin gel
JP2005501952A JP4379813B2 (en) 2002-09-27 2003-09-26 Reduced gel polystyrene resin separation and recovery equipment
PCT/JP2003/012310 WO2004029113A1 (en) 2002-09-27 2003-09-26 Apparatus for the separation and recovery of volume-reduced polystyrene resin gel
AT03748594T ATE489213T1 (en) 2002-09-27 2003-09-26 DEVICE FOR SEPARATING AND RECOVERING REDUCED VOLUME POLYSTYRENE RESIN GEL
DE60335126T DE60335126D1 (en) 2002-09-27 2003-09-26 DEVICE FOR SEPARATING AND OBTAINING VOLUME REDUCED POLYSTYRENE ROLLING GEL
EP20030748594 EP1550676B1 (en) 2002-09-27 2003-09-26 Apparatus for the separation and recovery of volume-reduced polystyrene resin gel
TW92126905A TWI311572B (en) 2002-09-27 2003-09-26 Apparatus for treating volume-reduced polystyrene resin in gel state for material separation and recovery

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PCT/JP2002/010098 WO2004029140A1 (en) 2002-09-27 2002-09-27 Volume-decreased gel-like polystyrene resin separating and recovering device

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1194440A (en) * 1968-11-19 1970-06-10 Mitsui Toatsu Chemicals Improvements in or relating to the Removal of Volatile Substances from Viscous Compositions
JPS62179508A (en) * 1986-02-03 1987-08-06 Mitsui Toatsu Chem Inc Removal of volatile matter
JPH03137901A (en) * 1989-10-25 1991-06-12 Nakayama Kankyo Enji Kk Evaporator
JPH093239A (en) * 1995-06-19 1997-01-07 Ube Ind Ltd Treatment of styrene synthetic resin waste and method for recycling
JP2000119439A (en) * 1998-08-10 2000-04-25 Shin Nippon Engineering Kk Solid matter separation apparatus
JP2001310971A (en) * 2000-04-27 2001-11-06 Takayoshi Yamada Apparatus for separating and recovering waste expanded polystyrene after reducing volume

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1194440A (en) * 1968-11-19 1970-06-10 Mitsui Toatsu Chemicals Improvements in or relating to the Removal of Volatile Substances from Viscous Compositions
JPS62179508A (en) * 1986-02-03 1987-08-06 Mitsui Toatsu Chem Inc Removal of volatile matter
JPH03137901A (en) * 1989-10-25 1991-06-12 Nakayama Kankyo Enji Kk Evaporator
JPH093239A (en) * 1995-06-19 1997-01-07 Ube Ind Ltd Treatment of styrene synthetic resin waste and method for recycling
JP2000119439A (en) * 1998-08-10 2000-04-25 Shin Nippon Engineering Kk Solid matter separation apparatus
JP2001310971A (en) * 2000-04-27 2001-11-06 Takayoshi Yamada Apparatus for separating and recovering waste expanded polystyrene after reducing volume

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