JP2006263727A - Mixing and pulverizing device, mixing and melting method, and method of molding cellulose material impregnated with binder - Google Patents
Mixing and pulverizing device, mixing and melting method, and method of molding cellulose material impregnated with binder Download PDFInfo
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- 239000000463 material Substances 0.000 title claims abstract description 236
- 239000011230 binding agent Substances 0.000 title claims abstract description 68
- 238000000034 method Methods 0.000 title claims abstract description 60
- 238000002844 melting Methods 0.000 title claims abstract description 54
- 230000008018 melting Effects 0.000 title claims abstract description 53
- 238000010298 pulverizing process Methods 0.000 title claims abstract description 45
- 229920002678 cellulose Polymers 0.000 title claims description 17
- 239000001913 cellulose Substances 0.000 title claims description 17
- 238000000465 moulding Methods 0.000 title description 11
- 239000010908 plant waste Substances 0.000 claims abstract description 24
- 238000007906 compression Methods 0.000 claims abstract description 16
- 230000006835 compression Effects 0.000 claims abstract description 16
- 238000010008 shearing Methods 0.000 claims abstract description 16
- 239000002023 wood Substances 0.000 claims description 39
- 239000002916 wood waste Substances 0.000 claims description 29
- 238000001035 drying Methods 0.000 claims description 16
- 238000000227 grinding Methods 0.000 claims description 16
- 230000008859 change Effects 0.000 claims description 10
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- 238000004891 communication Methods 0.000 claims description 7
- 239000002826 coolant Substances 0.000 claims description 5
- 238000000605 extraction Methods 0.000 claims description 5
- 238000001125 extrusion Methods 0.000 claims description 5
- 230000001052 transient effect Effects 0.000 claims description 5
- 239000002801 charged material Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 230000007423 decrease Effects 0.000 claims description 3
- 238000005470 impregnation Methods 0.000 claims 1
- 238000012544 monitoring process Methods 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000011049 filling Methods 0.000 abstract description 6
- 230000020169 heat generation Effects 0.000 abstract description 4
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 19
- 241000218645 Cedrus Species 0.000 description 16
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- 238000005469 granulation Methods 0.000 description 10
- 230000003179 granulation Effects 0.000 description 10
- 239000012778 molding material Substances 0.000 description 9
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- 241000218691 Cupressaceae Species 0.000 description 8
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 8
- 241000018646 Pinus brutia Species 0.000 description 8
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- 230000000052 comparative effect Effects 0.000 description 8
- 230000018044 dehydration Effects 0.000 description 8
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- 238000010438 heat treatment Methods 0.000 description 8
- 210000004027 cell Anatomy 0.000 description 6
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- 241000218652 Larix Species 0.000 description 5
- 235000005590 Larix decidua Nutrition 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 229920006167 biodegradable resin Polymers 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 235000013312 flour Nutrition 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 229920003002 synthetic resin Polymers 0.000 description 3
- 239000000057 synthetic resin Substances 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- 235000011201 Ginkgo Nutrition 0.000 description 2
- 244000194101 Ginkgo biloba Species 0.000 description 2
- 235000008100 Ginkgo biloba Nutrition 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 241000219000 Populus Species 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000010903 husk Substances 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
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- 235000009566 rice Nutrition 0.000 description 2
- 241000167854 Bourreria succulenta Species 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241001412225 Firmiana simplex Species 0.000 description 1
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- 244000269722 Thea sinensis Species 0.000 description 1
- 229920002522 Wood fibre Polymers 0.000 description 1
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- 230000005611 electricity Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000035943 smell Effects 0.000 description 1
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Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
- Debarking, Splitting, And Disintegration Of Timber (AREA)
- Crushing And Pulverization Processes (AREA)
- Accessories For Mixers (AREA)
Abstract
Description
本発明は、セルロース系材料、すなわち木質材料及び植物材料を高い比率で利用するためのあるいは木質廃材及び植物廃材を高い比率で再利用するための混合粉砕装置、混合溶融方法及びバインダーが含浸されたセルロース系材料の成形方法に関するものである。 The present invention is impregnated with a mixing and pulverizing apparatus, a mixing and melting method, and a binder for using cellulosic materials, that is, wood materials and plant materials in a high ratio or for recycling wood waste materials and plant waste materials in a high ratio. The present invention relates to a method for molding a cellulosic material.
合成樹脂の意匠性付与の手段として木粉を合成樹脂に練り込む方法がとられているが、合成樹脂と木粉は一般的に相溶性に乏しく、従来市販されている大半の木粉充填成形材料の木粉充填比率は重量比で50%を少し超えているのが現状である。 Although the method of kneading wood powder into synthetic resin is used as a means of imparting design properties of synthetic resin, synthetic resin and wood powder are generally poorly compatible, and most of the wood powder filling molding that has been commercially available in the past The present condition is that the wood powder filling ratio of the material slightly exceeds 50% by weight.
従来の木粉充填成形材料の製造方法は、単純混合と呼ばれていて、スギ、ヒノキ、マツ等の人工乾燥後の含水率が12%以下の粒度150μm前後の木粉を使用し、熱蒸気またはオイルにて約160℃程度に熱した混合溶融機に前述した木粉を重量比で50%入れ、混合羽根を回転させ約20分程乾燥し含水率を0.3%以下にする。その後、バインダーとして熱可塑性樹脂(PP、PE、生分解性樹脂など)、相溶化剤(反応性ポリオレフィン系オリゴマー、無水マレイン酸など)等を重量比で50%入れ混合羽根を約20分程回転させ単純混合させるものであった。その後、ゲル状の混合品を冷却機(冷却水:20℃、流量:100L/min)に入れ約15分程羽根を回転させ冷却造粒するものであった。 A conventional method for producing a wood-filled molding material is called simple mixing, and uses wood flour having a particle size of about 150 μm with a moisture content of 12% or less after artificial drying, such as cedar, cypress, and pine. Alternatively, 50% by weight of the above-mentioned wood flour is put into a mixing and melting machine heated to about 160 ° C. with oil, and the mixing blade is rotated and dried for about 20 minutes to reduce the water content to 0.3% or less. Then, add 50% by weight of thermoplastic resin (PP, PE, biodegradable resin, etc.), compatibilizer (reactive polyolefin oligomer, maleic anhydride, etc.) as binder and rotate the mixing blade for about 20 minutes. And was simply mixed. Thereafter, the gel-like mixture was put into a cooler (cooling water: 20 ° C., flow rate: 100 L / min), and the blades were rotated for about 15 minutes to cool and granulate.
いずれも市販品の木粉を使用して乾燥工程、混合溶融工程および造粒工程の各工程を経て製造しているのであり、材料の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、溶融混合、造粒を全て一工程(混合溶融装置一台)で行うものでなく、しかも短い熱履歴で処理できるものではなく、廃材については再利用までの環境負荷が大きく、コスト面及び生産性の面で問題があった。 All of them are manufactured through the dry process, mixing and melting process and granulation process using commercially available wood flour, and in a state of being fragmented without worrying about the moisture content of the material at all. If it is, fine grinding, drying, melt mixing, and granulation are not all performed in one process (one mixing and melting device), and it cannot be processed with a short heat history. There was a problem in terms of cost and productivity.
そこで本発明者は、駆動源によって回転駆動され、回転自在に支持された回転軸に複数の羽根部材が配設され材料の混合粉砕が行われる混合容器を備えた混合粉砕装置において、材料投入部に対応する回転軸に投入された材料を前記混合容器に供給するらせん状羽根部材が配設され、前記複数の羽根部材は、前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された少なくとも2個の羽根部材によって構成され、前記羽根部材の前記回転軸に対する取付け角は、前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一であり、前記混合容器の側壁に該混合容器内で混合粉砕された材料を取り出す取出部が配設され、前記混合容器内において、前記木質材料およびまたは植物材料および前記バインダーが混合粉砕され、剪断、摩擦および圧縮による発熱により含有水分が脱水された前記木質材料およびまたは植物材料に溶融した前記バインダーが含浸されるという本発明の第1の技術的思想に着眼した。 In view of this, the inventor of the present invention provides a material input unit in a mixing and pulverizing apparatus including a mixing container in which a plurality of blade members are arranged on a rotating shaft that is rotatably driven by a driving source and performs mixing and pulverization of materials. And a plurality of blade members are arranged in the axial direction at a constant angular interval in the circumferential direction of the rotation shaft. It is composed of at least two blade members disposed on the rotation shaft so as to face each other and have a mounting angle that narrows the facing distance in the rotation direction. The mounting angle of the blade member with respect to the rotation shaft is the rotation angle. An extraction portion for taking out the material mixed and crushed in the mixing vessel is disposed on the side wall of the mixing vessel, which is the same from the root portion attached to the shaft to the radially outer tip portion. In the mixing container, the wood material and / or the plant material and the binder are mixed and pulverized, and the wood material and / or the plant material melted in the wood material and / or the plant material dehydrated by heat generated by shearing, friction and compression is impregnated. We focused on the first technical idea of the present invention.
また本発明者は、駆動源によって回転駆動される回転軸に配設された複数の羽根部材によって混合容器内においてセルロース系材料の混合粉砕が行われる混合溶融方法において、材料投入部より投入された小片化したセルロース系材料およびバインダーが、前記混合容器内の前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内における前記セルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出されるという本発明の第2の技術的思想に着眼した。 In addition, the inventor of the present invention introduced a material charging unit in a mixing and melting method in which mixing and pulverization of a cellulosic material is performed in a mixing container by a plurality of blade members arranged on a rotating shaft that is driven to rotate by a driving source. The fragmented cellulosic material and the binder are opposed to each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft in the mixing container, and the mounting angle is such that the facing interval is reduced in the rotating direction. It is mixed and pulverized by at least two blade members disposed on the rotating shaft, and melted into the cellulose-based material from which water content has been dehydrated by heat generation due to shearing, friction and compression of the cellulose-based material in the mixing container. When the cellulosic material is impregnated with a molten binder, And focusing on the second technical idea of the present invention that is taken out from within.
本発明は、材料の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、脱水混合、造粒を全て一工程(混合溶融装置一台)でそれも短い熱履歴で処理できるものであり、廃材については再利用までの環境負荷が小さく、コスト面及び生産性の面を改善することを目的とするものである。
本発明においては、トチノキ、イチョウ、アオギリ、サクラ、ヤナギ、ポプラ等の街路樹として植えられている木々の剪定枝葉やスギ、ヒノキ、マツ、カラマツ等の剪定枝葉、スギ、ヒノキ、マツ、カラマツ等の間伐材、スギ、ヒノキ、マツ、カラマツ等の樹皮、製材所から出るスギ、ヒノキ、マツ等の端材やおがくず、集成材等の木質材および木質廃材、ならびに小麦の茎や葉、お茶の葉、籾殻等の植物材および植物廃材等のセルロース系材料の含水率など全く気にする事無く、小片化または細片化した状態であれば微粉砕、乾燥、溶融混合、造粒を全て一工程(混合溶融装置一台)でそれも短い熱履歴で処理できるようにするもので、利用および再利用までの環境負荷が少ないものである。
The present invention does not care about the moisture content of the material at all, and if it is in a fragmented state, fine grinding, drying, dehydration mixing, and granulation are all performed in one step (one mixing and melting device), which also has a short heat history The purpose of the waste materials is to reduce the environmental load until reuse, and to improve the cost and productivity.
In the present invention, pruned branches and leaves of trees planted as roadside trees such as Japanese cypress, ginkgo, green grass, cherry blossom, willow, poplar, etc., pruned branches and leaves of cedar, cypress, pine, larch, etc. Thinned timber, bark of cedar, cypress, pine, larch, etc., milled timber from timber, cypress, pine, etc. If you are shredded or shredded without worrying about the moisture content of cellulosic materials such as leaves and rice husks and plant wastes, all of them are finely pulverized, dried, melt mixed and granulated. In the process (one mixing and melting apparatus), it can be processed with a short heat history, and the environmental load until use and reuse is small.
また本発明は、従来の技術ではコスト面及び生産性の面で問題となっていた、剪定枝葉等の木質端廃材および木質廃材及び小麦の茎や葉等の植物材および植物廃材の有効利用および再利用法を提供し、廃材の高充填化により使用率を増大させ廃材の再利用の促進を進めるものである。 In addition, the present invention has been a problem in terms of cost and productivity in the prior art, effective utilization of wood edge waste materials such as pruned branches and leaves and wood waste materials, plant materials such as wheat stems and leaves, and plant waste materials and A recycling method will be provided, and the utilization rate will be increased by increasing the filling of waste materials to promote the reuse of waste materials.
本発明(請求項1に記載の第1発明)の混合粉砕装置は、
駆動源によって回転駆動され、回転自在に支持された回転軸に複数の羽根部材が配設され材料の混合粉砕が行われる混合容器を備えた混合粉砕装置において、
材料投入部に対応する回転軸に、投入された材料を前記混合容器に供給するらせん状羽根部材が配設され、
前記複数の羽根部材は、前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された少なくとも2個の羽根部材によって構成され、
前記羽根部材の前記回転軸に対する取付け角は、前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一であり、
前記混合容器の側壁に該混合容器内で混合粉砕された材料を取り出す取出部が配設され、
前記混合容器内において、前記材料が混合粉砕される
ものである。
The mixing and grinding apparatus of the present invention (first invention according to claim 1) is:
In a mixing and pulverizing apparatus including a mixing container in which a plurality of blade members are arranged on a rotation shaft that is rotationally driven by a driving source and rotatably supported, and the material is mixed and pulverized.
A spiral blade member for supplying the charged material to the mixing container is disposed on the rotation shaft corresponding to the material charging portion,
The plurality of blade members are arranged on the rotary shaft at an attachment angle so as to face each other in the axial direction at a portion having a constant angular interval in the circumferential direction of the rotary shaft and to narrow the mutual spacing in the rotational direction. Constituted by at least two blade members;
The mounting angle of the blade member with respect to the rotating shaft is the same from the root portion attached to the rotating shaft to the radially outer tip.
An extraction portion for taking out the material mixed and ground in the mixing container is disposed on the side wall of the mixing container,
In the mixing container, the material is mixed and ground.
本発明(請求項2に記載の第2発明)の混合粉砕装置は、
前記第1発明において、
前記羽根部材が、矩形の板状部材によって構成されている
ものである。
The mixing and grinding apparatus of the present invention (the second invention according to claim 2)
In the first invention,
The said blade member is comprised by the rectangular plate-shaped member.
本発明(請求項3に記載の第3発明)の混合粉砕装置は、
前記第2発明において、
前記駆動源が、前記回転軸にベルトその他の回転連絡手段を介して連絡するモータによって構成されている
ものである。
The mixing and grinding apparatus of the present invention (the third invention according to claim 3)
In the second invention,
The drive source is constituted by a motor that communicates with the rotation shaft via a belt or other rotation communication means.
本発明(請求項4に記載の第4発明)の混合粉砕装置は、
前記第3発明において、
冷却媒体を、前記回転軸の一端から他端に供給するとともに、混合容器の壁内に供給循環させる冷却装置を備えている
ものである。
The mixing and grinding apparatus of the present invention (the fourth invention according to claim 4) is:
In the third invention,
A cooling medium is supplied from one end of the rotating shaft to the other end, and is provided with a cooling device for supplying and circulating the cooling medium in the wall of the mixing container.
本発明(請求項5に記載の第5発明)の混合粉砕装置は、
前記第4発明において、
前記回転軸の両端を軸支する軸受け部に、該軸受け部の軸方向の両端を連通する溝が形成され、
前記混合容器内における前記材料の剪断、摩擦および圧縮による発熱により脱水された脱水成分の排出を可能にするように構成されものである。
The mixing and grinding apparatus of the present invention (the fifth invention according to claim 5) is:
In the fourth invention,
A groove that communicates both ends of the bearing portion in the axial direction is formed in the bearing portion that supports both ends of the rotating shaft,
The dewatering component dehydrated by heat generated by shearing, friction and compression of the material in the mixing container is configured to be discharged.
本発明(請求項6に記載の第6発明)の混合粉砕装置は、
前記第5発明において、
前記混合容器内における材料の混合粉砕および乾燥状態に応じた前記モータの主軸に作用する負荷トルクの変化に基づき、前記混合容器の前記取出部に配設された開閉部材の開閉を制御して、混合粉砕された材料を取り出す開閉制御装置を備えている
ものである。
The mixing and pulverizing apparatus of the present invention (the sixth invention according to claim 6) is:
In the fifth invention,
Based on the change of the load torque acting on the main shaft of the motor according to the mixing and pulverization and drying state of the material in the mixing container, controlling the opening and closing of the opening and closing member disposed in the take-out portion of the mixing container, An opening / closing control device for taking out the mixed and pulverized material is provided.
本発明(請求項7に記載の第7発明)の混合溶融方法は、
駆動源によって回転駆動される回転軸に配設された複数の羽根部材によって混合容器内においてセルロース系材料の混合粉砕が行われる混合溶融方法において、
材料投入部より投入された小片化したセルロース系材料およびバインダーが、前記混合容器内の前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記回転軸に対する取付け角が前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一である少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内における前記セルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、
前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出される
ものである。
The mixing and melting method of the present invention (the seventh invention according to claim 7) is:
In the mixing and melting method in which the mixing and pulverization of the cellulosic material is performed in the mixing container by the plurality of blade members disposed on the rotating shaft that is rotationally driven by the driving source,
The fragmented cellulosic material and the binder charged from the material charging part face each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft in the mixing container, and also face each other in the rotating direction. At least two blade members that are disposed on the rotary shaft at a mounting angle such that the mounting angle with respect to the rotary shaft is the same from a root portion that is attached to the rotary shaft to a radially outer tip. Mixed and pulverized, impregnated with a molten binder in the cellulosic material dehydrated by heat generated by shearing, friction and compression of the cellulosic material in the mixing vessel,
Once the cellulosic material is impregnated with the molten binder, it is taken out from the mixing container.
本発明(請求項8に記載の第8発明)の混合溶融方法は、
前記第7発明において、
前記セルロース系材料が、前記木質材料およびまたは植物材料である
ものである。
The mixing and melting method of the present invention (the eighth invention according to claim 8) is:
In the seventh invention,
The cellulosic material is the wood material and / or plant material.
本発明(請求項9に記載の第9発明)の混合溶融方法は、
前記第8発明において、
前記木質材料およびまたは植物材料が、前記木質廃材およびまたは植物廃材である
ものである。
The mixing and melting method of the present invention (the ninth invention according to claim 9)
In the eighth invention,
The wood material and / or plant material is the wood waste material and / or plant waste material.
本発明(請求項10に記載の第10発明)の混合溶融方法は、
前記第9発明において、
前記羽根部材の先端周速が、毎秒5メートルないし毎秒50メートルの範囲内になるように前記駆動源としてのモータによって前記回転軸が回転駆動されている
ものである。
The mixing and melting method of the present invention (the tenth invention according to claim 10)
In the ninth invention,
The rotary shaft is rotationally driven by a motor as the drive source so that the tip peripheral speed of the blade member is in the range of 5 meters per second to 50 meters per second.
本発明(請求項11に記載の第11発明)の混合溶融方法は、
前記第10発明において、
前記モータと前記回転軸とは、急激な過渡的回転変動には追従しないように回転連絡されている
ものである。
The mixing and melting method of the present invention (the eleventh invention according to claim 11)
In the tenth invention,
The motor and the rotating shaft are in rotation communication so as not to follow a rapid transient rotational fluctuation.
本発明(請求項12に記載の第12発明)の混合溶融方法は、
前記第11発明において、
前記モータの主軸に作用する負荷トルクの変化を監視する
ものである。
The mixing and melting method of the present invention (the twelfth aspect of the invention described in claim 12)
In the eleventh aspect,
A change in load torque acting on the main shaft of the motor is monitored.
本発明(請求項13に記載の第13発明)の混合溶融方法は、
前記第12発明において、
監視している前記モータの主軸に作用する負荷トルクが、前記混合容器内における材料の混合粉砕および乾燥状態に応じて前記モータの主軸にかかる負荷トルクが上昇して最大値に達した後低下して最小値に達した後、一定時間経過したら、前記混合容器の取出部より混合粉砕、脱水され前記バインダーが含浸された前記セルロース系材料を取り出す
ものである。
The mixing and melting method of the present invention (the thirteenth aspect of the present invention) is
In the twelfth invention,
The load torque acting on the main shaft of the motor being monitored decreases after the load torque applied to the main shaft of the motor increases and reaches a maximum value according to the mixing and pulverization and drying state of the material in the mixing container. When a certain time has elapsed after reaching the minimum value, the cellulosic material impregnated with the binder is taken out from the take-out portion of the mixing container.
本発明(請求項14に記載の第14発明)のバインダーが含浸されたセルロース系材料の成形方法は、
材料投入部より投入された小片化したセルロース系材料およびバインダーが、混合容器内の駆動源によって回転駆動される回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記回転軸に対する取付け角が前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一である少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内におけるセルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、
前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出され、
前記混合容器内から取り出された溶融した前記バインダーが含浸された前記セルロース系材料を加熱および加圧することにより成形する
ものである。
The molding method of the cellulosic material impregnated with the binder of the present invention (14th invention according to claim 14)
The cellulosic material and the binder that are put into pieces from the material feeding unit face each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft that is driven to rotate by the drive source in the mixing container, and the rotational direction. And at least two mounting angles that are the same from the root portion that is attached to the rotating shaft to the distal end portion in the radial direction. In the mixing container, the melted binder is impregnated with the cellulosic material mixed and pulverized and dehydrated by heat generated by shearing, friction and compression of the cellulosic material in the mixing container,
Once the cellulosic material is impregnated with molten binder, it is removed from the mixing container,
The cellulosic material impregnated with the molten binder taken out from the mixing container is molded by heating and pressurizing.
本発明(請求項15に記載の第15発明)のバインダーが含浸されたセルロース系材料の成形方法は、
前記第14発明において、
前記バインダーが含浸された前記セルロース系材料の成形が、押出成形によって行われる
ものである。
The molding method of the cellulosic material impregnated with the binder of the present invention (the fifteenth invention according to claim 15)
In the fourteenth aspect,
The cellulosic material impregnated with the binder is molded by extrusion molding.
本発明(請求項16に記載の第16発明)のバインダーが含浸されたセルロース系材料の成形方法は、
前記第15発明において、
前記セルロース系材料が、前記木質廃材およびまたは植物廃材である
ものである。
The molding method of the cellulosic material impregnated with the binder of the present invention (the sixteenth invention according to claim 16)
In the fifteenth aspect of the invention,
The cellulosic material is the wood waste and / or plant waste.
上記構成より成る第1発明の混合粉砕装置は、駆動源によって回転駆動され、回転自在に支持された回転軸に複数の羽根部材が配設され材料の混合粉砕が行われる混合容器を備えた混合粉砕装置において、材料投入部に対応する回転軸に、投入された材料を前記混合容器に供給するらせん状羽根部材が配設され、前記複数の羽根部材は、前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された少なくとも2個の羽根部材によって構成され、前記羽根部材の前記回転軸に対する取付け角は、前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一であり、前記混合容器の側壁に該混合容器内で混合粉砕された材料を取り出す取出部が配設され、前記混合容器内において、前記材料が混合粉砕され、剪断、摩擦および圧縮による発熱により前記材料の含有水分が脱水されるので、材料の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、脱水混合、造粒を全て一工程(混合粉砕装置一台)でそれも短い熱履歴で処理できるものであり、廃材については再利用までの環境負荷が小さく、コスト面及び生産性の問題を解消するという効果を奏する。 The mixing and pulverizing apparatus according to the first aspect of the present invention having the above-described configuration is a mixing device provided with a mixing container in which a plurality of blade members are disposed on a rotating shaft rotatably supported by a driving source and mixed and pulverized. In the pulverizing apparatus, a spiral blade member for supplying the charged material to the mixing container is disposed on a rotation shaft corresponding to the material charging portion, and the plurality of blade members are fixed in a circumferential direction of the rotation shaft. The rotation of the blade member is configured by at least two blade members disposed on the rotation shaft at an attachment angle so as to face each other in the axial direction at an angular interval portion and to narrow the mutual interval in the rotation direction. The angle of attachment to the shaft is the same from the root portion attached to the rotating shaft to the radially outer tip, and the material mixed and ground in the side wall of the mixing vessel in the mixing vessel In the mixing container, the material is mixed and pulverized, and the moisture content of the material is dehydrated by heat generated by shearing, friction and compression, so the moisture content of the material is completely concerned. If it is in a small state, fine grinding, drying, dehydration mixing, and granulation can be processed in a single process (one mixing and grinding device) with a short heat history, and waste materials can be reused. The environmental load is small, and there is an effect that the problem of cost and productivity is solved.
上記構成より成る第2発明の混合粉砕装置は、前記第1発明において、前記羽根部材が、矩形の板状部材によって構成されているので、シンプルな構成によって 前記材料の混合粉砕および脱水を実現し、保守を容易にして、寿命を伸ばすという効果を奏する。 In the mixing and pulverizing apparatus of the second invention configured as described above, in the first invention, the blade member is constituted by a rectangular plate-like member, so that mixing and dehydration of the material is realized with a simple structure. This makes it easy to maintain and prolong the service life.
上記構成より成る第3発明の混合粉砕装置は、前記第2発明において、前記駆動源が、前記回転軸にベルトその他の回転連絡手段を介して連絡するモータによって構成されているので、前記駆動源を構成する前記モータの配置の自由度が高いという効果を奏する。 In the mixing and grinding apparatus of the third invention having the above-described configuration, in the second invention, the drive source is constituted by a motor that communicates with the rotating shaft via a belt or other rotation communication means. There is an effect that the degree of freedom of the arrangement of the motors constituting the motor is high.
上記構成より成る第4発明の混合粉砕装置は、前記第3発明において、前記冷却装置が、冷却媒体を前記回転軸の一端から他端に供給するとともに、混合容器の壁内に供給循環させるので、前記回転軸および混合容器の壁を冷却して温度上昇を抑制するという効果を奏する。 In the mixing and pulverizing apparatus according to a fourth aspect of the present invention having the above-described configuration, in the third aspect of the invention, the cooling device supplies and circulates a cooling medium from one end of the rotating shaft to the other end and circulates in the wall of the mixing container. The rotating shaft and the wall of the mixing container are cooled, and the temperature rise is suppressed.
上記構成より成る第5発明の混合粉砕装置は、前記第4発明において、前記回転軸の両端を軸支する軸受け部に形成された前記軸受け部の軸方向の両端を連通する溝によって、前記混合容器内における前記材料の剪断、摩擦および圧縮による発熱により脱水された脱水成分の排出を可能にするという効果を奏する。 According to a fifth aspect of the present invention, there is provided the mixing and pulverizing apparatus according to the fourth aspect, wherein the mixing and pulverizing apparatus includes the groove formed in the bearing portion that pivotally supports both ends of the rotary shaft, and the groove that communicates both axial ends of the bearing portion. There is an effect that it is possible to discharge a dehydrated component dehydrated by heat generated by shearing, friction and compression of the material in the container.
上記構成より成る第6発明の混合粉砕装置は、前記第5発明において、前記開閉制御装置が、前記混合容器内における材料の混合粉砕および乾燥状態に応じた前記モータの主軸に作用する負荷トルクの変化に基づき、前記混合容器の前記取出部に配設された開閉部材の開閉を制御して、混合粉砕された材料を取り出すので、含有水分が脱水された前記材料の取り出しを可能にするという効果を奏する。 The mixing and pulverizing apparatus of the sixth invention configured as described above is the mixing and pulverizing apparatus according to the fifth aspect of the present invention, wherein the opening / closing control device has Based on the change, the opening and closing member disposed in the take-out portion of the mixing container is controlled to take out the mixed and pulverized material, so that the material dehydrated in water can be taken out. Play.
上記構成より成る第7発明の混合溶融方法は、駆動源によって回転駆動される回転軸に配設された複数の羽根部材によって混合容器内においてセルロース系材料の混合粉砕が行われる混合溶融方法において、材料投入部より投入された小片化したセルロース系材料およびバインダーが、前記混合容器内の前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記回転軸に対する取付け角が前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一である少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内における前記セルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出されるので、脱水された前記セルロース系材料にバインダーが均一に含浸されるため、前記セルロース系材料の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、脱水混合、造粒を全て一工程(混合溶融装置一台)でそれも短い熱履歴で処理できるものであり、廃材については成形材としての再利用までの環境負荷が小さく、コスト面及び生産性の問題を解消するという効果を奏する。 The mixing and melting method of the seventh invention having the above-described configuration is a mixing and melting method in which mixing and pulverization of a cellulosic material is performed in a mixing container by a plurality of blade members disposed on a rotating shaft that is rotationally driven by a driving source. The fragmented cellulosic material and the binder charged from the material charging part face each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft in the mixing container, and also face each other in the rotating direction. At least two blade members that are disposed on the rotary shaft at a mounting angle such that the mounting angle with respect to the rotary shaft is the same from a root portion that is attached to the rotary shaft to a radially outer tip. The mixed water is dehydrated by heat generation due to shearing, friction and compression of the cellulosic material in the mixing container. When the melted binder is impregnated into the cellulosic material, and the melted binder is impregnated into the cellulosic material, the dehydrated cellulosic material is uniformly impregnated with the binder because it is taken out from the mixing container. Therefore, without worrying about the water content of the cellulosic material at all, if it is in a fragmented state, fine pulverization, drying, dehydration mixing, and granulation are all performed in one step (one mixing and melting apparatus), which is also short. It can be processed by heat history, and the waste material has an effect that the environmental load until reuse as a molding material is small, and the problem of cost and productivity is solved.
上記構成より成る第8発明の混合溶融方法は、前記第7発明において、前記セルロース系材料が、前記木質材料およびまたは植物材料であるので、脱水された前記木質材料およびまたは植物材料にバインダーが均一に含浸されるため、前記木質材料およびまたは植物材料の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、脱水混合、造粒を全て一工程(混合溶融装置一台)でそれも短い熱履歴で処理できるものであり、廃材については成形材としての再利用までの環境負荷が小さく、コスト面及び生産性の問題を解消するという効果を奏する。 In the mixing and melting method of the eighth invention having the above structure, in the seventh invention, since the cellulosic material is the wood material and / or plant material, the binder is uniformly formed on the dehydrated wood material and / or plant material. Therefore, fine grinding, drying, dehydration mixing, and granulation are all carried out in one step (one mixing and melting device) without worrying about the moisture content of the woody material and / or plant material. It can be processed with a short heat history, and the waste material has the effect of reducing the environmental load until reuse as a molding material and eliminating the problem of cost and productivity.
上記構成より成る第9発明の混合溶融方法は、前記第8発明において、前記木質材料およびまたは植物材料が、前記木質廃材およびまたは植物廃材であるので、脱水された前記木質廃材およびまたは植物廃材にバインダーが均一に含浸されるため、前記木質廃材およびまたは植物廃材の含水率など全く気にする事無く、小片化した状態であれば微粉砕、乾燥、脱水混合、造粒を全て一工程(混合溶融装置一台)でそれも短い熱履歴で処理できるものであり、廃材については成形材としての再利用までの環境負荷が小さく、コスト面及び生産性の問題を解消するという効果を奏する。 In the mixing and melting method of the ninth invention having the above structure, in the eighth invention, the wood material and / or plant material is the wood waste material and / or plant waste material. Since the binder is uniformly impregnated, the pulverization, drying, dehydration mixing, and granulation are all performed in one step (mixing) as long as it is fragmented without worrying about the moisture content of the wood waste and / or plant waste. One melting apparatus) can also be processed with a short heat history, and the waste material has a small environmental load until reuse as a molding material, and has the effect of eliminating the problem of cost and productivity.
上記構成より成る第10発明の混合溶融方法は、前記第9発明において、前記羽根部材の先端周速が、毎秒5メートルないし毎秒50メートル の範囲内になるように前記駆動源としてのモータによって前記回転軸が回転駆動されているので、前記混合容器内における微粉砕、乾燥、脱水混合、造粒を望ましい状態において行うことが出来るという効果を奏する。 The mixing and melting method of the tenth aspect of the present invention having the above-described structure is the method according to the ninth aspect, wherein the tip peripheral speed of the blade member is within a range of 5 meters / second to 50 meters / second by the motor as the drive source. Since the rotating shaft is driven to rotate, there is an effect that fine pulverization, drying, dehydration mixing and granulation in the mixing container can be performed in a desired state.
上記構成より成る第11発明の混合溶融方法は、前記第10発明において、前記モータと前記回転軸とは、急激な過渡的回転変動には追従しないように回転連絡されているので、前記混合容器内における回転している羽根部材に作用している負荷トルクの急激な過渡的変化をモータの主軸に作用しないようにしたので、モータの寿命を伸ばすという効果を奏する In the mixing and melting method according to the eleventh aspect of the present invention, in the tenth aspect, the motor and the rotary shaft are in rotational communication so as not to follow a rapid transient rotational fluctuation. Since a sudden and transient change of the load torque acting on the rotating blade member inside the motor is prevented from acting on the main shaft of the motor, there is an effect of extending the life of the motor.
上記構成より成る第12発明の混合溶融方法は、前記第11発明において、前記モータの主軸に作用する負荷トルクの変化を監視するので、前記混合容器内における微粉砕、乾燥、脱水混合、造粒の状態を把握することが出来るという効果を奏する。 In the mixing and melting method of the twelfth aspect of the present invention, the change in load torque acting on the main shaft of the motor is monitored in the eleventh aspect of the invention, so fine pulverization, drying, dehydration mixing, and granulation in the mixing container There is an effect that it is possible to grasp the state of.
上記構成より成る第13発明の混合溶融方法は、前記第12発明において、監視している前記モータの主軸に作用する負荷トルクが、前記混合容器内における材料の混合粉砕および乾燥状態に応じて前記モータの主軸にかかる負荷トルクが上昇して最大値に達した後低下して最小値に達した後、一定時間経過したら、前記混合容器の取出部より混合粉砕、脱水されバインダーが含浸された前記セルロース系材料を取り出すので、脱水された前記セルロース系材料の生成を可能にするという効果を奏する。 In the mixing and melting method of the thirteenth aspect of the present invention configured as described above, in the twelfth aspect of the invention, the load torque acting on the main shaft of the motor being monitored depends on the mixing and pulverization and drying state of the material in the mixing container. The load torque applied to the main shaft of the motor rises and reaches a maximum value and then decreases and reaches a minimum value.After a certain time has elapsed, the mixture is crushed and dehydrated from the take-out portion of the mixing container and impregnated with the binder. Since the cellulosic material is taken out, there is an effect that the dehydrated cellulosic material can be produced.
上記構成より成る第14発明のバインダーが含浸されたセルロース系材料の成形方法は、材料投入部より投入された小片化したセルロース系材料およびバインダーが、混合容器内の駆動源によって回転駆動される回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記回転軸に対する取付け角が前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一である少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内におけるセルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出され、前記混合容器内から取り出された溶融した前記バインダーが含浸された前記セルロース系材料を加熱および加圧することにより成形するので、溶融した前記バインダーが含浸された前記セルロース系材料の強固な成形品を得ることが出来るという効果を奏する。 According to the fourteenth aspect of the present invention, there is provided a method for molding a cellulose-based material impregnated with a binder, wherein the cellulose-based material and the binder, which are put into pieces from the material charging unit, are rotated by a driving source in a mixing container. The rotating shafts are opposed to each other in the axial direction at a constant angular interval in the circumferential direction of the shaft, and are disposed on the rotating shaft at a mounting angle that narrows the facing interval in the rotating direction. The mixed water is pulverized by at least two blade members that are the same from the root portion attached to the shaft to the radially outer tip portion, and the moisture content is generated by heat generation due to shearing, friction and compression of the cellulosic material in the mixing container. The dehydrated cellulosic material is impregnated with a molten binder, and the cellulosic material is melted with a molten bath. When the binder is impregnated, the cellulosic material taken out from the mixing container and impregnated with the molten binder taken out from the mixing container is molded by heating and pressurizing. There is an effect that a strong molded product of the impregnated cellulosic material can be obtained.
上記構成より成る第15発明のバインダーが含浸されたセルロース系材料の成形方法は、前記第14発明において、前記バインダーが含浸された前記セルロース系材料の成形が、押出成形によって行われるので、溶融した前記バインダーが含浸された前記セルロース系材料の強固な成形品の連続成形を可能にするという効果を奏する。 The method for molding a cellulose material impregnated with the binder according to the fifteenth aspect of the present invention is melted because the molding of the cellulose material impregnated with the binder is performed by extrusion molding in the fourteenth aspect of the invention. There is an effect that it is possible to continuously form a strong molded article of the cellulosic material impregnated with the binder.
上記構成より成る第16発明のバインダーが含浸されたセルロース系材料の成形方法は、前記第15発明において、前記セルロース系材料が、前記木質廃材およびまたは植物廃材であるので、前記木質廃材およびまたは植物廃材による強固な成形品の連続成形を可能にするという効果を奏する。 The method for molding a cellulose material impregnated with the binder according to the sixteenth aspect of the present invention is the method according to the fifteenth aspect, wherein the cellulose material is the wooden waste material and / or the plant waste material. There is an effect that it is possible to continuously form a strong molded product with waste materials.
以下本発明の実施の形態につき、図面を用いて具体的に説明する。 Embodiments of the present invention will be specifically described below with reference to the drawings.
本第1実施形態の混合粉砕装置および該混合粉砕装置を用いた混合溶融方法は、図1および図2に示されるように駆動源としてのモータ8によって回転駆動され、回転自在に支持された回転軸5に複数の羽根部材10aないし10fが配設され材料の混合粉砕が行われる混合容器3を備えた混合粉砕装置において、材料投入部に対応する回転軸に投入された材料を前記混合容器に供給するらせん状羽根部材12が配設され、前記複数の羽根部材10aないし10fの少なくとも2枚は、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸5に配設され、前記混合容器3の側壁に該混合容器内で混合粉砕された材料を取り出す取出部17が配設され、前記混合容器3内において、前記材料が混合粉砕され、剪断、摩擦および圧縮による発熱により含有水分が脱水されるものである。 The mixing and pulverizing apparatus according to the first embodiment and the mixing and melting method using the mixing and pulverizing apparatus are driven to rotate by a motor 8 as a drive source as shown in FIG. 1 and FIG. In the mixing and pulverizing apparatus including the mixing container 3 in which a plurality of blade members 10a to 10f are arranged on the shaft 5 and the materials are mixed and pulverized, the material input to the rotating shaft corresponding to the material input unit is supplied to the mixing container. A spiral blade member 12 to be supplied is disposed, and at least two of the plurality of blade members 10a to 10f are disposed on the rotary shaft 5 at an attachment angle such that a spacing between the blade members 10a to 10f is reduced in the rotation direction. An extraction portion 17 for taking out the material mixed and pulverized in the mixing container is disposed on the side wall of the mixing container 3, and in the mixing container 3, the material is mixed and pulverized, and shearing, friction and It is those containing water is dehydrated by heat generated by condensation.
本第1実施形態においては、セルロース系材料としての細片化した木質廃材及び植物廃材とバインダーの熱可塑性樹脂(PP、PE、生分解性樹脂など)、相溶化剤(反応性ポリオレフィン系オリゴマー、無水マレイン酸など)等と共に前記らせん状羽根部材12を介して前記混合容器3内に供給し、相対する複数の回転羽根10aないし10fの高速回転により、細片化した木質廃材及び植物廃材とバインダーが高速で衝突を繰り返す。 In the first embodiment, the wood waste material and plant waste material as cellulosic materials and binder thermoplastic resin (PP, PE, biodegradable resin, etc.), compatibilizer (reactive polyolefin oligomer, Wood waste material and plant waste material and binder which are supplied into the mixing container 3 through the spiral blade member 12 together with maleic anhydride and the like, and are spun into pieces by high-speed rotation of a plurality of opposed rotary blades 10a to 10f. Repeats collisions at high speed.
この際の前記混合容器3内における木質廃材及び植物廃材の挙動は、未だ学術的に必ずしも明らかにになっているものではないが、その時の衝突エネルギーにより、細片物から微粉砕物となり、最終的に微粉粒となり、その間の衝突エネルギーは内部エネルギーに変換され、微粉粒それ自体の温度上昇が起こる。 At this time, the behavior of the wood waste material and the plant waste material in the mixing container 3 has not yet been clarified academically, but the impact energy at that time changes the fine product into a finely pulverized product. The impact energy in the meantime is converted into internal energy, and the temperature of the fine powder itself increases.
また同時期に包囲された前記混合容器3の内面に微粉粒を押し付けるように打撃しかつ押し進める前記回転羽根12の作用による熱運動効果(内部摩擦加熱)が起こり、前記した内部エネルギーによる温度上昇と相乗的に働き、同時に回転羽根軸に連続的に設けた後述する脱水成分排出用の溝を介して材料混合容器3内へ空気が大量に流入し、急激な温度上昇(約1、2秒の間に60℃→200℃超)が起こる事になる。 Further, a thermal motion effect (internal frictional heating) occurs due to the action of the rotary blade 12 that strikes and pushes the fine particles against the inner surface of the mixing vessel 3 surrounded at the same time, and the temperature rise due to the internal energy described above. A large amount of air flows into the material mixing container 3 through a groove for discharging a dehydrating component, which will be described later, which works synergistically and is continuously provided on the rotating blade shaft, and a rapid temperature rise (approximately 1 to 2 seconds) In the meantime, 60 ° C. → over 200 ° C.) occurs.
従来の技術において記載した単純混合と異なり、前記混合容器3内が一瞬のうちに高温高圧の状態となり、細胞内腔や細胞間隙等の空隙中に存在する自由水と、細胞壁中に含まれている結合水が抜けた隙間に、木材においてセルロースに次いで多い割合のリグニンが媒介となりバインダーの熱可塑性樹脂(PP、PE、生分解性樹脂など)、相溶化剤(反応性ポリオレフィン系オリゴマー、無水マレイン酸など)が入り込み単純混合では全く見られない木材を構成するセルロース等と均一にそして強い結合力を持って一体化するのである(図面8の写真)。すなわち前記リグニンは、3つのモノグリノールの重合体からなる3次元網目状構造をした天然高分子であり、バインダーの高分子との親和性によって脱水状態のセルロース成分に溶融したバインダーが含浸されたと考えることが出来る。 Unlike the simple mixing described in the prior art, the inside of the mixing container 3 is in a high temperature and high pressure state in an instant, and is contained in free water existing in voids such as cell lumens and cell gaps, and in cell walls. In the gaps where the bound water is removed, the second largest proportion of lignin after cellulose in the wood mediates binder thermoplastic resins (PP, PE, biodegradable resins, etc.), compatibilizers (reactive polyolefin oligomers, maleic anhydride) Acid, etc.) enters and integrates with cellulose, etc., which constitutes wood, which cannot be seen by simple mixing, uniformly and with a strong bonding force (photo of FIG. 8). That is, the lignin is a natural polymer having a three-dimensional network structure made of three monoglycol polymers, and it is considered that the dehydrated cellulose component is impregnated with the melted binder due to the affinity of the binder polymer. I can do it.
したがって、前記混合容器3から取り出された脱水状態のセルロース成分に溶融したバインダーが含浸され微細片によって、木質廃材及び植物廃材の比率が重量比で80%〜90%の高充填成形材料の製造を可能にするとともに、工程を単純化することができ、コスト面及び生産性の面で大きな効果が得られることを可能にするものである。 Therefore, the dehydrated cellulose component taken out from the mixing container 3 is impregnated with the melted binder to produce a highly filled molding material in which the ratio of the wood waste material and the plant waste material is 80% to 90% by weight. In addition, the process can be simplified and a great effect can be obtained in terms of cost and productivity.
第2実施形態の混合粉砕装置は、図1ないし図6に示されるように駆動源によって回転駆動され、回転自在に支持された回転軸5に複数の羽根部材10aなしい10fが配設され材料の混合粉砕が行われる混合容器3を備えた混合粉砕装置において、材料投入部14に対応する回転軸5に投入された木質材料およびまたは植物材料およびバインダーを前記混合容器3に供給するらせん状羽根部材12が配設され、前記複数の羽根部材は、前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された複数の羽根部材によって構成され、前記羽根部材の前記回転軸に対する取付け角は、前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一であり、前記混合容器3の側壁に該混合容器内で混合粉砕された材料を取り出す取出部17が配設され、前記混合容器内において、前記材料が混合粉砕され、剪断、摩擦および圧縮による発熱により含有水分が脱水され、含有水分が脱水された前記木質材料およびまたは植物材料に溶融した前記バインダーが含浸されるものである。 As shown in FIGS. 1 to 6, the mixing and pulverizing apparatus of the second embodiment is rotationally driven by a driving source, and a plurality of blade members 10a and 10f are arranged on a rotating shaft 5 that is rotatably supported. In the mixing and pulverizing apparatus including the mixing container 3 in which the mixing and pulverization is performed, the spiral blades that supply the wooden material and / or the plant material and the binder charged into the rotating shaft 5 corresponding to the material charging unit 14 to the mixing container 3 The member 12 is disposed, and the plurality of blade members are opposed to each other in the axial direction at a portion having a constant angular interval in the circumferential direction of the rotating shaft, and the mounting angle is such that the opposing interval is narrowed in the rotating direction. It is constituted by a plurality of blade members arranged on the rotation shaft, and the mounting angle of the blade member with respect to the rotation shaft is a radial direction from the root portion attached to the rotation shaft. An extraction portion 17 for taking out the material mixed and pulverized in the mixing container is disposed on the side wall of the mixing container 3, and the material is mixed and pulverized in the mixing container. The water content is dehydrated by heat generated by shearing, friction and compression, and the wood material and / or plant material from which the water content has been dehydrated are impregnated with the binder.
本第2実施形態の混合粉砕装置について、図面を用いて具体的に説明する。図1において、一例としての混合溶融装置1を示す。この混合溶融装置1においては、機台ベース2上に横向に円筒形の混合容器3と、前記材料投入部14および前記らせん状羽根部材12が配設される供給容器13が複数の脚部によって配置される。 The mixing and grinding apparatus according to the second embodiment will be specifically described with reference to the drawings. FIG. 1 shows a mixing and melting apparatus 1 as an example. In this mixing and melting apparatus 1, a cylindrical mixing container 3 on a machine base 2 and a supply container 13 in which the material charging part 14 and the spiral blade member 12 are disposed are constituted by a plurality of legs. Be placed.
両端の脚部に配置された軸受4,4により回転羽根軸5を水平に支持して、該回転羽根軸5が該混合容器3の中心と同軸的に貫挿配置され、該回転羽根軸5の一端(図1中右端)をプーリー6とVベルト7を介して駆動源としてのモーター8と回転連絡している。 The rotating blade shaft 5 is horizontally supported by the bearings 4 and 4 disposed at the leg portions at both ends, and the rotating blade shaft 5 is coaxially inserted through the center of the mixing container 3. One end (right end in FIG. 1) is in rotational communication with a motor 8 as a drive source via a pulley 6 and a V belt 7.
回転羽根軸5は、軸心部に冷却水供給用の小径の孔部が形成された中空状であり、その両端にロータリージョイント9が設けられ、該ロータリージョイント9を通して冷却水を該回転羽根軸5の内部に軸方向に供給するように構成されている。 The rotary blade shaft 5 has a hollow shape in which a small-diameter hole for supplying cooling water is formed in an axial center portion, and rotary joints 9 are provided at both ends thereof, and cooling water is supplied to the rotary blade shaft through the rotary joint 9. 5 is configured to be supplied in the axial direction.
混合容器3中を貫通して配置された回転羽根軸5の外周には図2に示されるように計6枚の横断面形状矩形であるとともに、全体形状矩形の羽根10a〜10fが、前記回転軸の円周方向の180度の角度間隔の部位における軸方向において対向して突設されている。羽根10a〜10fの厚さは、図2に示されるように外周側略4割の部分が内周側に比べて厚く形成されており、材料の混合、粉砕および溶融が、効果的に行われるように構成されている。 As shown in FIG. 2, the outer periphery of the rotary blade shaft 5 penetrating the mixing container 3 has a total of six cross-sectional rectangles, and the blades 10a to 10f having an overall shape are rotated as described above. The projections are opposed to each other in the axial direction at portions having an angular interval of 180 degrees in the circumferential direction of the shaft. As shown in FIG. 2, the thickness of the blades 10a to 10f is approximately 40% of the outer peripheral side thicker than that of the inner peripheral side, so that the mixing, crushing, and melting of the materials are performed effectively. It is configured as follows.
そのうちの軸方向の両端部の羽根10a及び10fは図1の右側面から見た場合の時計回りに回転したとき、その前縁が混合容器3の両端の垂直壁11,11の内面と殆ど隙間なく摺接するように羽根の先端から根元まで約15度の取付け角度で傾斜して回転羽根軸5の外周に固着されている。 When the blades 10a and 10f at both ends in the axial direction are rotated clockwise as viewed from the right side of FIG. 1, the leading edges thereof are almost spaced from the inner surfaces of the vertical walls 11 and 11 at both ends of the mixing vessel 3. The blade is fixed to the outer periphery of the rotary blade shaft 5 at an attachment angle of about 15 degrees from the tip of the blade to the base so as to be in sliding contact.
また中間部の4枚の羽根10b、10c、10d、10eは回転羽根軸5の外周面に千鳥状に各羽根の先端から根元まで約15度の角度で傾斜して固着され回転時の前縁が該混合容器3の両端を向く方向に各々配置されている。すなわち4枚の羽根10bおよび10d、10cおよび10eは、図2および図6に示されるように軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角(円周方向に対する角度)は15度になるように前記回転軸5に配設されている。 The four blades 10b, 10c, 10d, and 10e in the middle part are fixed to the outer peripheral surface of the rotary blade shaft 5 in a staggered manner at an angle of about 15 degrees from the tip of each blade to the root, and the leading edge during rotation. Are arranged in a direction facing both ends of the mixing container 3. That is, the four blades 10b and 10d, 10c and 10e are opposed to each other in the axial direction as shown in FIGS. 2 and 6, and the mounting angle (the angle with respect to the circumferential direction) is such that the facing distance in the rotational direction is narrowed. ) Is arranged on the rotary shaft 5 so as to be 15 degrees.
また、前記混合容器3の両端壁11のモーター側は、該混合容器3の一方の端壁に開設された混合容器3の材料供給口であり、12は、回転羽根軸5の外周に形成された螺旋状の材料供給スクリューであり、13は、該供給スクリュー12を包囲している材料供給箱、14は、該材料供給箱13の上方に設けられたホッパーであり、該ホッパー14には材料を投入した後混合粉砕溶融時には気密に閉止し得る開閉自在のシャッター15が設けられている。また両側一対の16,16は、回転羽根軸5に固設された円滑な回転を得るためのバランスホイールである。 Further, the motor side of both end walls 11 of the mixing container 3 is a material supply port of the mixing container 3 opened on one end wall of the mixing container 3, and 12 is formed on the outer periphery of the rotary blade shaft 5. A helical material supply screw, 13 is a material supply box surrounding the supply screw 12, and 14 is a hopper provided above the material supply box 13. An openable and closable shutter 15 is provided that can be hermetically closed when mixing, pulverizing and melting after the slag is added. Further, a pair of both sides 16 and 16 are balance wheels for obtaining a smooth rotation fixed to the rotary blade shaft 5.
混合容器3の周壁中には連続した通水路が形成され、冷却水を循環させることにより該混合容器3を冷却し得るように構成されている。また、17は、混合容器3の底壁部に設けられた造粒された材料を取り出すための排出口蓋で、該排出口蓋17は、軸18により回転可能に支持され該軸18はロータリーシリンダー19、19と連結され、開閉できるように構成されている。
また、図2に示される両側のカラー20、20は、空気を混合容器3に送るためのもので回転羽根軸5の回転により空気が混合容器3に送られるように両端の各々の連続した溝は右ネジ、左ネジの螺旋溝で構成されている。
A continuous water passage is formed in the peripheral wall of the mixing vessel 3, and the mixing vessel 3 can be cooled by circulating cooling water. Reference numeral 17 denotes a discharge port lid provided on the bottom wall portion of the mixing container 3 for taking out the granulated material. The discharge port cover 17 is rotatably supported by a shaft 18, and the shaft 18 is a rotary cylinder 19. , 19 so that it can be opened and closed.
Also, the collars 20, 20 on both sides shown in FIG. 2 are for sending air to the mixing container 3, and each continuous groove at both ends is so that air is sent to the mixing container 3 by the rotation of the rotary blade shaft 5. Is composed of right and left spiral grooves.
また、21は制御盤で、前記モーター8と接続ケーブルを介して連結されており、該モーター8より主軸の負荷トルクが連続的に電気信号として該制御盤21に入力されるように構成されている。
前記混合容器3内における材料の混合粉砕および乾燥状態に応じた前記モータ8の主軸に作用する負荷トルクの変化に基づき、前記混合容器3の前記取出部に配設された開閉部材17の開閉のタイミングを制御して、混合粉砕された材料を取り出す開閉制御装置を備えているものである。
Reference numeral 21 denotes a control panel, which is connected to the motor 8 via a connection cable, and is configured such that the load torque of the main shaft is continuously input from the motor 8 to the control panel 21 as an electrical signal. Yes.
Based on the change of the load torque acting on the main shaft of the motor 8 according to the mixing and pulverization of the material in the mixing container 3 and the dry state, the opening and closing member 17 disposed in the take-out portion of the mixing container 3 is opened and closed. An opening / closing control device for controlling the timing and taking out the mixed and pulverized material is provided.
上記構成より成る混合溶融装置を用いた本第2実施形態の混合溶融方法は、駆動源としてのモータ8によって回転駆動される回転軸5に配設された複数の羽根部材10a〜10fによって混合容器内においてセルロース系材料である木質材料およびまたは植物材料の混合粉砕が行われる混合溶融方法において、材料投入部より投入された小片化したセルロース系材料としての木質材料およびまたは植物材料およびバインダーが、前記混合容器3内の前記回転軸5の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸5に配設された少なくとも2個の羽根部材によって、混合粉砕され、該混合容器3内における前記セルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、前記セルロース系材料としての木質材料およびまたは植物材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出されるものである。 In the mixing and melting method of the second embodiment using the mixing and melting apparatus having the above-described configuration, a mixing container is provided by a plurality of blade members 10a to 10f disposed on a rotary shaft 5 that is rotationally driven by a motor 8 as a drive source. In the mixing and melting method in which the wood material and / or plant material which is a cellulosic material is mixed and pulverized, the wood material and / or the plant material and the binder as the fragmented cellulosic material charged from the material charging unit are The rotating shaft 5 in the mixing container 3 is disposed on the rotating shaft 5 at an attachment angle so as to face each other in the axial direction at a certain angular interval in the circumferential direction and to narrow the facing interval in the rotating direction. The cellulosic material is mixed and pulverized by at least two blade members, and the cellulosic material in the mixing container 3 is sheared, rubbed and frictioned. When the melted binder is impregnated into the cellulosic material dehydrated by heat generated by compression and the wood material and / or plant material as the cellulosic material is impregnated with the molten binder, the cellulosic material is taken out from the mixing container. It is what
前記セルロース系材料は、前記木質材料およびまたは植物材料であり、前記木質材料およびまたは植物材料は、前記木質廃材およびまたは植物廃材を用いて再利用することが出来る。
すなわち、前記木質廃材およびまたは植物廃材は、トチノキ、イチョウ、アオギリ、サクラ、ヤナギ、ポプラ等の街路樹として植えられている木々の剪定枝葉やスギ、ヒノキ、マツ、カラマツ等の剪定枝葉、スギ、ヒノキ、マツ、カラマツ等の間伐材、スギ、ヒノキ、マツ、カラマツ等の樹皮、製材所から出るスギ、ヒノキ、マツ等の端材やおがくず、集成材等の木質材および木質廃材、ならびに小麦の茎や葉、お茶の葉、籾殻等の植物材および植物廃材等のセルロース系材料の含水率など全く気にする事無く、小片化または細片化した状態のものであれば良いのである。
The cellulosic material is the wood material and / or plant material, and the wood material and / or plant material can be reused using the wood waste material and / or plant waste material.
That is, the wood waste material and / or plant waste material is pruned branches and leaves of trees planted as street trees such as Tochinoki, Ginkgo, Aogiri, Sakura, Willow, Poplar, etc., pruned branches and leaves of cedar, cypress, pine, larch, etc. Thinned timber, pine, larch, etc., bark such as cedar, cypress, pine, larch, etc., wood and wood waste such as sawwood, cypress, pine, etc. Any material that is in the state of being fragmented or fragmented may be used without worrying about the moisture content of cellulosic materials such as stems, leaves, tea leaves, rice husks and the like and plant waste materials.
前記羽根部材10a〜10fの先端周速が、毎秒5メートルないし毎秒50メートルの範囲内になるように前記駆動源としてのモータ8によって前記回転軸が回転駆動されており、前記モータ8と前記回転軸5とは、急激な過渡的回転変動には追従しないように回転連絡されており、前記モータ8の主軸に作用する負荷トルクの変化を監視して、図7に示されるように監視している前記モータ8の主軸に作用する負荷トルクが、前記混合容器3内における材料の混合粉砕および乾燥状態に応じて前記モータ8の主軸にかかる負荷トルクTが上昇して最大値Xに達した後低下して最小値Iに達した後、一定時間tが経過したら、前記混合容器3の取出部17より混合粉砕、脱水され前記バインダーが含浸された前記セルロース系材料としての前記木質廃材およびまたは植物廃材を取り出すものである。 The rotating shaft is rotationally driven by the motor 8 as the driving source so that the tip peripheral speed of the blade members 10a to 10f is in the range of 5 meters per second to 50 meters per second. The shaft 5 is rotationally connected so as not to follow a sudden transient rotational fluctuation, and the change of the load torque acting on the main shaft of the motor 8 is monitored and monitored as shown in FIG. After the load torque acting on the main shaft of the motor 8 reaches the maximum value X, the load torque T applied to the main shaft of the motor 8 increases according to the mixing and pulverization and drying state of the material in the mixing container 3. After reaching a minimum value I after decreasing, when a certain time t has elapsed, the cellulose-based material before mixing and pulverizing from the take-out part 17 of the mixing container 3 and dehydrating and impregnating the binder is obtained. It is intended to take out the wood waste material and or plant wastes.
このように本第2実施形態の混合溶融装置および混合溶融方法は、木質廃材及び植物廃材を再利用するもので、木の風合いがあり、木の香りがする、静電気の発生が少ないとともに、紫外線吸収後の物性低下が少なく、水分呼吸をする等により木に近い成形品を得るための原材料を提供するものである。 As described above, the mixing and melting apparatus and the mixing and melting method according to the second embodiment recycles the wood waste material and the plant waste material, has a texture of wood, smells of wood, generates less static electricity, and emits ultraviolet rays. The present invention provides a raw material for obtaining a molded product close to wood by, for example, less breathing of moisture after absorption and breathing moisture.
また既存の成形機、金型、二次加工用木工機が、そのまま使用できるため特殊な設備は全く必要がないとともに、木質廃材及び植物廃材を細片化した状態から微粉砕、乾燥、溶融混合、造粒を短時間に全て一工程、すなわち混合溶融装置一台でこなし、外部加熱を一切使用していないので、製造コストを大幅に低減でき、バインダーに生分解性樹脂を使用することにより、より自然にやさしい成形品を得ることが出来る。 In addition, since existing molding machines, molds, and woodworking machines for secondary processing can be used as they are, no special equipment is required. In addition, wood waste and plant waste are finely pulverized, dried, and melt mixed. , Granulation is done in one step in a short time, that is, with one mixing and melting device, and no external heating is used, so the manufacturing cost can be greatly reduced, and by using a biodegradable resin for the binder, More naturally friendly molded products can be obtained.
また製造過程で発生する不良品等も粉砕し、100%利用して成形が可能で、繰返し再利用ができるとともに、また木質廃材及び植物廃材を高い比率で再利用するため、資源の有効利用の点で誠に有益な効果を奏するものである。 In addition, inferior goods generated in the manufacturing process can be crushed and molded using 100%, and can be reused repeatedly. In addition, because wood waste and plant waste are reused at a high rate, effective use of resources can be achieved. This is a very beneficial effect.
すなわち、本第2実施形態においては、前記混合容器3内において上記加熱処理を施した木質材料が、自己接着性と熱流動性を発現することを利用するもので、前記混合容器3内において蒸気加熱した木質材料を前記開閉部材17を一気に開けることにより解圧して一旦乾燥させ、蒸気爆砕生成物を熱プレス等により加熱、加圧することにより、成形体を作製できるのである。 That is, in the second embodiment, the wood material subjected to the heat treatment in the mixing container 3 utilizes the fact that self-adhesiveness and thermal fluidity are expressed. The heated wood material is depressurized by opening the opening / closing member 17 at once, dried once, and the molded product can be produced by heating and pressurizing the steam explosion product with a hot press or the like.
蒸気加熱処理した木質材料は、接着性成分を保有し、接着剤無しで成形できるとともに、加熱、加圧することにより、流動することが分かっている。木質材料だけを原料として、強固なプラスチック様の成形体を製造することが出来るものである。 It has been found that a wood material subjected to steam heat treatment has an adhesive component, can be molded without an adhesive, and flows when heated and pressurized. A strong plastic-like molded body can be produced using only a woody material as a raw material.
以下本発明の実施例につき、図面を用いて説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1実施例の混合溶融装置1および混合溶融方法は、図1および図3に示されるように回転羽根軸5の内部を軸方向に及び混合容器3の壁部内に鉢巻き状に各々冷却水を循環させて、回転羽根軸5および混合容器3を冷却する。
モーター8により該回転羽根軸5を介して羽根10a〜10fを回転させる。羽根10a〜10fの先端速度が毎秒約5mの状態において、事前計量してホッパー14に装填している細片化した木質廃材(スギ:重量比85%)とバインダー(PP:重量比12%、無水マレイン酸:3%)をシャッター15を開いて材料供給箱13へ供給した後、シャッター15を閉じる。そして供給スクリュー12の回転により混合容器3内に材料が供給押し入れられる。
In the mixing and melting apparatus 1 and the mixing and melting method of the first embodiment, as shown in FIGS. 1 and 3, the cooling water is respectively supplied in the axial direction inside the rotary blade shaft 5 and in a headband shape in the wall portion of the mixing container 3. The rotary blade shaft 5 and the mixing container 3 are cooled by circulation.
The blades 10 a to 10 f are rotated by the motor 8 through the rotating blade shaft 5. In a state where the tip speed of the blades 10a to 10f is about 5 m per second, the wood waste material that has been preliminarily weighed and loaded into the hopper 14 (cedar: 85% by weight) and binder (PP: 12% by weight, After the shutter 15 is opened and supplied to the material supply box 13, the shutter 15 is closed. Then, the material is supplied and pushed into the mixing container 3 by the rotation of the supply screw 12.
すなわち、ホッパー14が空になったらシャッター15を閉め、羽根10a〜10fの先端速度が毎秒約30mになるまで該モーター8の回転を上げていき、羽根10a〜10fの先端速度が毎秒約30mの状態において約40秒ほど維持する。 That is, when the hopper 14 is empty, the shutter 15 is closed, and the rotation of the motor 8 is increased until the tip speed of the blades 10a to 10f reaches about 30 m per second, and the tip speed of the blades 10a to 10f is about 30 m per second. The state is maintained for about 40 seconds.
この間に材料が細片物工程、微粉砕物工程、微粉粒工程と進行し、その過程で材料に含まれていた水分が抜け、微粉粒は全乾状態に近い状態になり、内部エネルギーと内部摩擦加熱の相乗効果によって、一気に混合容器3内の温度が60℃から200℃を超える温度まで上昇する。
この時前記混合容器3内が一瞬のうちに高温高圧の状態となり、細胞内腔や細胞間隙等の空隙中に存在する自由水と、細胞壁中に含まれている結合水が抜けた隙間に、バインダーが一瞬のうちに溶融混合して木材を構成するセルロース等と均一にそして強い結合力を持って一体化する。
During this time, the material progresses into the fine particle process, the finely pulverized product process, and the fine particle process, and the moisture contained in the material is released in the process, and the fine particles become almost dry, and the internal energy and internal Due to the synergistic effect of frictional heating, the temperature in the mixing vessel 3 rises from 60 ° C. to over 200 ° C. at once.
At this time, the inside of the mixing container 3 is in a state of high temperature and high pressure in an instant, and the free water present in the void such as the cell lumen and the cell gap and the gap from which the bound water contained in the cell wall has been removed, The binder melts and mixes instantly and integrates with cellulose, etc., which constitutes the wood, uniformly and with a strong binding force.
材料が溶融混合するとき羽根10a〜10f及び回転羽根軸5に一瞬の内に大きな負荷トルクがかかる。本実施例においては、モーター8にかかるトルク数値で130%前後となる。高速で回転している羽根10a〜10f及び回転羽根軸5にブレーキがかかった状態になると、該回転羽根軸5側のプーリー6とモーター8側のプーリー6を連結しているVベルト7においてすべりが発生し、急激な負荷トルク変動をモーター8の主軸に伝えない構成になっている。 When the materials are melted and mixed, a large load torque is applied to the blades 10a to 10f and the rotary blade shaft 5 in a moment. In this embodiment, the torque value applied to the motor 8 is about 130%. When the blades 10a to 10f rotating at a high speed and the rotating blade shaft 5 are braked, slip occurs in the V belt 7 connecting the pulley 6 on the rotating blade shaft 5 side and the pulley 6 on the motor 8 side. And a sudden load torque fluctuation is not transmitted to the main shaft of the motor 8.
モーター8にかかる負荷トルクの変動を、電気信号に変換をして前記制御盤21に送り、該制御盤21内で予め入力しておいた負荷トルクデータと照合させ溶融混合の終了時期を読み取り、羽根10a〜10fの先端速度が毎秒約30mの高速回転の状態において、ロータリーシリンダー19、19を駆動させ、軸18を介して連結されている排出口蓋17を開き、脱水され、バインダーが含浸され造粒されたスギの高充填成形材料を排出する。 The fluctuation of the load torque applied to the motor 8 is converted into an electric signal and sent to the control panel 21 to be compared with the load torque data inputted in advance in the control panel 21 to read the end timing of the melt mixing. With the tip speed of the blades 10a to 10f rotating at a high speed of about 30 m per second, the rotary cylinders 19 and 19 are driven, the discharge port lid 17 connected through the shaft 18 is opened, dehydrated, and impregnated with a binder. Drain the high-filling molding material of grained cedar.
前記モーター8の負荷トルク変動の値は、木質廃材及び植物廃材の種類及び混合容器3内に入れる木質廃材及び植物廃材の重量等で違いが出るため、最初は手動にて混合溶融装置1を運転し、モーター8の負荷トルク変動の数値を読み取り制御盤21内にその数値を打込みデータベース化する必要があり、この予め格納されているデータに従い、前記排出口蓋17の開閉制御が行われる。 Since the value of the load torque fluctuation of the motor 8 differs depending on the types of wood waste and plant waste and the weight of the wood waste and plant waste put in the mixing container 3, the mixing and melting apparatus 1 is first operated manually. Then, it is necessary to read the numerical value of the load torque fluctuation of the motor 8 and input the numerical value into the control panel 21 to create a database, and the opening / closing control of the discharge port lid 17 is performed according to the data stored in advance.
本実施例におけるスギの高充填成形材料を用いて押出成形を行い、押出成形によって得られた成形品は、木質廃材(スギ:重量比85%)とバインダー(PP:重量比12%、無水マレイン酸:3%)である実施例について、各試験項目における各測定値を表1に示した。
比較例としてスギ材、比較例1(木質廃材55%、廃プラPP材30%、添加剤他15%)、比較例2(中密度ファィバーボード、木の繊維を利用し、接着剤を噴霧してホットプレスしたもの)および比較例3(木粉55%、樹脂45%)の各測定値も表1に示した。 As a comparative example, cedar wood, comparative example 1 (wood waste material 55%, waste plastic PP material 30%, additives and other 15%), comparative example 2 (medium density fiberboard, wood fibers, sprayed with adhesive Table 1 also shows the measured values of Comparative Example 3 (wood flour 55%, resin 45%).
表1からも明らかなようにスギ材の廃材を用いた実施例の硬さは、スギ材の2倍であり、縦圧縮強さは2割強であり、摩耗量は桁違いに少ないものである。 As is clear from Table 1, the hardness of the example using the cedar waste was twice that of the cedar, the longitudinal compressive strength was more than 20%, and the amount of wear was an order of magnitude less. is there.
また実施例の曲げヤング率は、比較例2および比較例3の略2倍であり、曲げ強さは、比較例2および比較例3に対してそれぞれ1割強、4割強である。
の数値にて示したものである。
Moreover, the bending Young's modulus of an Example is substantially 2 times of the comparative example 2 and the comparative example 3, and bending strength is slightly over 10% with respect to the comparative example 2 and the comparative example 3, respectively.
This is indicated by the numerical value.
図8に、本実施例に係わる高充填成形材料(木質廃材(スギ)+バインダー)の顕微鏡写真を示す。熱流動により仮道管(細胞)の配列がくずれ、バインダーが含浸されていることが分かる。 FIG. 8 shows a photomicrograph of the highly filled molding material (wood waste (cedar) + binder) according to this example. It can be seen that the arrangement of the temporary canals (cells) is disrupted by heat flow and the binder is impregnated.
図9に、本実施例に係わる木質廃材(スギ)の細片物の顕微鏡写真を示す。仮道管(細胞)が放射方向に整然と配列していることが分かる。木部の水分通導と樹体を機械的支持する両方の機能を兼務している。 FIG. 9 shows a photomicrograph of a strip of wood waste (cedar) according to this example. It can be seen that the temporary canals (cells) are arranged in an orderly manner in the radial direction. It combines the functions of moisture control of the xylem and mechanical support of the tree.
上述の実施形態は、説明のために例示したもので、本発明としてはそれらに限定されるものでは無く、特許請求の範囲、発明の詳細な説明および図面の記載から当業者が認識することができる本発明の技術的思想に反しない限り、変更および付加が可能である。 The above-described embodiments have been illustrated for the purpose of explanation, and the present invention is not limited thereto. Those skilled in the art will recognize from the claims, the detailed description of the invention, and the description of the drawings. Modifications and additions can be made without departing from the technical idea of the present invention.
また上述の実施形態および実施例においては、一例として取付け角15度の矩形の横断面形状の羽根部材について説明したが、本発明としてはそれらに限定されるものでは無く、例えば必要に応じて取付け角を15度以外の角度に設定することが出来るとともに、図10(A)および(B)に示されるように中間部分が凹および凸の翼形状の断面形状の羽根部材の実施形態を必要に応じて採用することが出来るものである。 In the above-described embodiments and examples, the blade member having a rectangular cross section with an attachment angle of 15 degrees has been described as an example. However, the present invention is not limited to these, and for example, attachment is performed as necessary. The angle can be set to an angle other than 15 degrees, and as shown in FIGS. 10A and 10B, an embodiment of a blade member having a wing-shaped cross section with a concave and convex intermediate portion is required. It can be adopted accordingly.
さらに上述の実施形態および実施例においては、一例としてロータリーシリンダーによって混合容器の排出口蓋を開閉する例について、説明したが、本発明としてはそれらに限定されるものでは無く、例えばシリンダー内をピストンが直線的に移動するピストンシリンダータイプのアクチュエータを用いて排出口蓋を開閉する実施形態を必要に応じて採用することが出来るものである。 Furthermore, in the above-described embodiments and examples, the example of opening and closing the discharge port lid of the mixing container by a rotary cylinder has been described as an example. However, the present invention is not limited thereto, and for example, a piston is provided in the cylinder. An embodiment in which the discharge port lid is opened and closed using a linearly moving piston-cylinder type actuator can be adopted as necessary.
また上述の実施形態および実施例においては、一例として混合容器内の混合、粉砕および溶融された材料の状態をモータの主軸保護の観点より、モータの主軸の負荷トルクに着目して検出する場合について説明したが、本発明としてはそれらに限定されるものでは無く、例えば混合容器内の温度や、混合容器の歪その他の混合容器内の混合、粉砕および溶融された材料の状態を反映する物理量を検出する実施形態を必要に応じて採用することが出来るものである。 In the above-described embodiments and examples, as an example, a case where the state of the mixed, pulverized, and melted material in the mixing container is detected by focusing on the load torque of the motor spindle from the viewpoint of protecting the spindle of the motor. As described above, the present invention is not limited to them. For example, the physical quantity reflecting the temperature in the mixing container, the distortion of the mixing container, and other mixed, pulverized and melted materials in the mixing container. The embodiment to be detected can be adopted as necessary.
駆動源としてのモータによって回転駆動され、回転自在に支持された回転軸に複数の羽根部材が配設され材料の混合粉砕が行われる混合容器を備えた混合粉砕装置および混合溶融方法において、材料投入部に対応する回転軸に投入された材料を前記混合容器に供給するらせん状羽根部材が配設され、前記複数の羽根部材の少なくとも2枚は、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記混合容器の側壁に該混合容器内で混合粉砕された材料が所定の状態に達したら材料を取り出す取出部が配設され、前記混合容器内において、前記材料が混合粉砕され、剪断、摩擦および圧縮による発熱により含有水分が脱水され、脱水された材料に溶融したバインダーを含浸させるもので、コスト面及び生産性の面で問題となっていた、剪定枝葉等の木質端廃材および木質廃材及び小麦の茎や葉等の植物材および植物廃材の有効利用および再利用法を提供し、廃材の高充填化により使用率を増大させ廃材の再利用の促進を進める用途に適用できるものである。 In a mixing and pulverizing apparatus and a mixing and melting method including a mixing container in which a plurality of blade members are arranged on a rotating shaft rotatably supported by a motor as a driving source and the materials are mixed and pulverized, and the mixing and melting method, the material is charged. A helical blade member that supplies the mixing container with the material charged to the rotating shaft corresponding to the portion is disposed, and at least two of the plurality of blade members are mounted such that the facing distance in the rotation direction is reduced. A corner is provided on the rotating shaft, and a take-out portion for taking out the material when the material mixed and ground in the mixing container reaches a predetermined state is disposed on the side wall of the mixing container. The material is mixed and pulverized, the water content is dehydrated by heat generated by shearing, friction and compression, and the dehydrated material is impregnated with a molten binder. We provide effective utilization and reuse methods for wood edge waste materials such as pruned branches and leaves, wood waste materials, plant materials such as wheat stems and leaves, and waste materials. It can be applied to applications that increase and promote the reuse of waste materials.
3 混合容器
5 回転羽根軸
8 モータ
17 排出口蓋
3 Mixing container 5 Rotating blade shaft 8 Motor 17 Discharge port lid
Claims (16)
材料投入部に対応する回転軸に、投入された材料を前記混合容器に供給するらせん状羽根部材が配設され、
前記複数の羽根部材は、前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設された少なくとも2個の羽根部材によって構成され、
前記羽根部材の前記回転軸に対する取付け角は、前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一であり、
前記混合容器の側壁に該混合容器内で混合粉砕された材料を取り出す取出部が配設され、
前記混合容器内において、前記材料が混合粉砕される
ことを特徴とする混合粉砕装置。 In a mixing and pulverizing apparatus including a mixing container in which a plurality of blade members are arranged on a rotation shaft that is rotationally driven by a driving source and rotatably supported, and the material is mixed and pulverized.
A spiral blade member for supplying the charged material to the mixing container is disposed on the rotation shaft corresponding to the material charging portion,
The plurality of blade members are arranged on the rotary shaft at an attachment angle so as to face each other in the axial direction at a portion having a constant angular interval in the circumferential direction of the rotary shaft and to narrow the mutual spacing in the rotational direction. Constituted by at least two blade members;
The mounting angle of the blade member with respect to the rotating shaft is the same from the root portion attached to the rotating shaft to the radially outer tip.
An extraction portion for taking out the material mixed and ground in the mixing container is disposed on the side wall of the mixing container,
A mixing and grinding apparatus, wherein the material is mixed and ground in the mixing container.
前記羽根部材が、矩形の板状部材によって構成されている
ことを特徴とする混合粉砕装置。 In claim 1,
The mixing and grinding apparatus, wherein the blade member is constituted by a rectangular plate-shaped member.
前記駆動源が、前記回転軸にベルトその他の回転連絡手段を介して連絡するモータによって構成されている
ことを特徴とする混合粉砕装置。 In claim 2,
The mixing and grinding apparatus, wherein the drive source is constituted by a motor that communicates with the rotating shaft via a belt or other rotational communication means.
冷却媒体を、前記回転軸の一端から他端に供給するとともに、混合容器の壁内に供給循環させる冷却装置を備えている
ことを特徴とする混合粉砕装置。 In claim 3,
A mixing and pulverizing apparatus, comprising: a cooling device that supplies a cooling medium from one end of the rotating shaft to the other end and supplies and circulates the cooling medium in the wall of the mixing container.
前記回転軸の両端を軸支する軸受け部に、該軸受け部の軸方向の両端を連通する溝が形成され、
前記混合容器内における前記材料の剪断、摩擦および圧縮による発熱により脱水された脱水成分の排出を可能にするように構成されている
ことを特徴とする混合粉砕装置。 In claim 4,
A groove that communicates both ends of the bearing portion in the axial direction is formed in the bearing portion that supports both ends of the rotating shaft,
A mixing and pulverizing apparatus configured to allow discharge of dehydrated components dehydrated by heat generated by shearing, friction and compression of the material in the mixing container.
前記混合容器内における材料の混合粉砕および乾燥状態に応じた前記モータの主軸に作用する負荷トルクの変化に基づき、前記混合容器の前記取出部に配設された開閉部材の開閉を制御して、混合粉砕された材料を取り出す開閉制御装置を備えている
ことを特徴とする混合粉砕装置。 In claim 5,
Based on the change of the load torque acting on the main shaft of the motor according to the mixing and pulverization and drying state of the material in the mixing container, controlling the opening and closing of the opening and closing member disposed in the take-out portion of the mixing container, A mixing and pulverizing apparatus comprising an opening / closing control device for taking out the mixed and pulverized material.
材料投入部より投入された小片化したセルロース系材料およびバインダーが、前記混合容器内の前記回転軸の円周方向の一定角度間隔の部位における軸方向において対向するとともに、回転方向において互いの対向間隔が狭まるような取付け角で前記回転軸に配設され、前記回転軸に対する取付け角が前記回転軸に取り付けられる根元部から半径方向外方の先端部まで同一である少なくとも2個の羽根部材によって、混合粉砕され、該混合容器内における前記セルロース系材料の剪断、摩擦および圧縮による発熱により含有水分が脱水された前記セルロース系材料に溶融したバインダーが含浸され、
前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出される
ことを特徴とする混合溶融方法。 In the mixing and melting method in which the mixing and pulverization of the cellulosic material is performed in the mixing container by the plurality of blade members disposed on the rotating shaft that is rotationally driven by the driving source,
The fragmented cellulosic material and the binder charged from the material charging part face each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft in the mixing container, and also face each other in the rotating direction. At least two blade members that are disposed on the rotary shaft at a mounting angle such that the mounting angle with respect to the rotary shaft is the same from a root portion that is attached to the rotary shaft to a radially outer tip. Mixed and pulverized, impregnated with a molten binder in the cellulosic material dehydrated by heat generated by shearing, friction and compression of the cellulosic material in the mixing vessel,
When the cellulosic material is impregnated with a molten binder, the mixing and melting method is taken out of the mixing container.
前記セルロース系材料が、前記木質材料およびまたは植物材料である
ことを特徴とする混合溶融方法。 In claim 7,
The mixing and melting method, wherein the cellulosic material is the wood material and / or plant material.
前記木質材料およびまたは植物材料が、前記木質廃材およびまたは植物廃材である
ことを特徴とする混合溶融方法。 In claim 8,
The mixing and melting method, wherein the wood material and / or plant material is the wood waste material and / or plant waste material.
前記羽根部材の先端周速が、毎秒5メートルないし毎秒50メートル
の範囲内になるように前記駆動源としてのモータによって前記回転軸が回転駆動されている
ことを特徴とする混合溶融方法。 In claim 9,
The mixing and melting method, wherein the rotating shaft is rotationally driven by a motor as the driving source so that a tip peripheral speed of the blade member is in a range of 5 meters per second to 50 meters per second.
前記モータと前記回転軸とは、急激な過渡的回転変動には追従しないように回転連絡されている
ことを特徴とする混合溶融方法。 In claim 10,
The mixing and melting method, wherein the motor and the rotating shaft are in rotational communication so as not to follow a rapid transient rotational fluctuation.
請求項5において、
前記モータの主軸に作用する負荷トルクの変化を監視する
ことを特徴とする混合溶融方法。 In claim 11,
In claim 5,
A mixing and melting method characterized by monitoring a change in load torque acting on the main shaft of the motor.
監視している前記モータの主軸に作用する負荷トルクが、前記混合容器内における材料の混合粉砕および乾燥状態に応じて前記モータの主軸にかかる負荷トルクが上昇して最大値に達した後低下して最小値に達した後、一定時間経過したら、前記混合容器の取出部より混合粉砕、脱水され前記バインダーが含浸された前記セルロース系材料を取り出す
ことを特徴とする混合溶融方法。 In claim 12,
The load torque acting on the main shaft of the motor being monitored decreases after the load torque applied to the main shaft of the motor increases and reaches a maximum value according to the mixing and pulverization and drying state of the material in the mixing container. Then, after a certain time has elapsed after reaching the minimum value, the cellulosic material impregnated with the binder after mixing, dewatering and impregnation is taken out from the take-out part of the mixing container.
前記セルロース系材料に溶融したバインダーが含浸されたら、前記混合容器内から取り出され、
前記混合容器内から取り出された溶融した前記バインダーが含浸された前記セルロース系材料を加熱および加圧することにより成形する
ことを特徴とする溶融したバインダーが含浸されたセルロース系材料の成形方法。 The cellulosic material and the binder that are put into pieces from the material feeding unit face each other in the axial direction at a constant angular interval in the circumferential direction of the rotating shaft that is driven to rotate by the drive source in the mixing container, and the rotational direction. And at least two mounting angles that are the same from the root portion that is attached to the rotating shaft to the distal end portion in the radial direction. In the mixing container, the melted binder is impregnated with the cellulosic material mixed and pulverized and dehydrated by heat generated by shearing, friction and compression of the cellulosic material in the mixing container,
Once the cellulosic material is impregnated with molten binder, it is removed from the mixing container,
A method for forming a cellulosic material impregnated with a molten binder, wherein the cellulosic material impregnated with the molten binder taken out of the mixing container is heated and pressurized.
前記バインダーが含浸された前記セルロース系材料の成形が、押出成形によって行われる
ことを特徴とする溶融したバインダーが含浸されたセルロース系材料の成形方法。 In claim 14,
A method for forming a cellulosic material impregnated with a molten binder, wherein the cellulosic material impregnated with the binder is formed by extrusion molding.
前記セルロース系材料が、前記木質廃材およびまたは植物廃材である
ことを特徴とするバインダーが含浸されたセルロース系材料の成形方法。 In claim 15,
A method for forming a cellulose-based material impregnated with a binder, wherein the cellulose-based material is the wood waste material and / or the plant waste material.
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JP2008194598A (en) * | 2007-02-09 | 2008-08-28 | Yukihisa Kato | Solid-liquid separator and solid-liquid separation method utilizing this separator |
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JP2008194598A (en) * | 2007-02-09 | 2008-08-28 | Yukihisa Kato | Solid-liquid separator and solid-liquid separation method utilizing this separator |
JP2009210156A (en) * | 2008-02-29 | 2009-09-17 | Mitsuo Naruse | Solid-liquid separation device and solid-liquid separating method using the same |
JPWO2010047358A1 (en) * | 2008-10-23 | 2012-03-22 | 独立行政法人科学技術振興機構 | Concentrated acid treatment section, concentrated acid treatment method, plant resource phase separation system conversion device and conversion method |
JP5633742B2 (en) * | 2008-10-23 | 2014-12-03 | 独立行政法人科学技術振興機構 | Concentrated acid treatment section, concentrated acid treatment method, plant resource phase separation system conversion device and conversion method |
KR200456307Y1 (en) | 2009-07-22 | 2011-10-21 | 김광희 | Appratus for shattering of spice |
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CN112121916A (en) * | 2020-09-30 | 2020-12-25 | 宜都国阳机电设备有限公司 | Shearing pendulum type breaking hammer |
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