JP7399208B2 - Spraying device for spraying liquid containing fine fibers and spraying method using a spraying device for spraying liquid containing fine fibers - Google Patents

Spraying device for spraying liquid containing fine fibers and spraying method using a spraying device for spraying liquid containing fine fibers Download PDF

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JP7399208B2
JP7399208B2 JP2022060774A JP2022060774A JP7399208B2 JP 7399208 B2 JP7399208 B2 JP 7399208B2 JP 2022060774 A JP2022060774 A JP 2022060774A JP 2022060774 A JP2022060774 A JP 2022060774A JP 7399208 B2 JP7399208 B2 JP 7399208B2
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慶郎 伊東
総平 萩原
優衣 林
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Chuetsu Pulp and Paper Co Ltd
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本発明は、微細状繊維を含む散布液の散布装置及び微細状繊維を含む散布液の散布装置を用いた散布方法に関する。 The present invention relates to a spraying device for a spraying liquid containing fine fibers and a spraying method using the spraying device for a spraying liquid containing fine fibers.

近年、耕種農業や畜産農業等の農業分野全般において、収穫量の増大や畜舎の環境を改善する等の様々な用途のために、各種散布装置を使用して、農場や畜舎等に、各種有効成分を含有する散布液を散布・噴霧している。 In recent years, in the general agricultural field such as arable farming and livestock farming, various types of spraying equipment have been used to spread various effective effects on farms and livestock barns for various purposes such as increasing yields and improving the environment of livestock barns. Spreading/spraying a spray liquid containing ingredients.

本願出願人は、特許文献1に、環境負荷が小さく安全性の高い噴霧剤として活用できる植物栽培剤を提供するという課題を解決するために、セルロースナノ繊維を含有し、植物に直接または間接に添加若しくは散布または噴霧され、殺虫有効成分がセルロースナノ繊維である植物栽培剤を開示した。 In order to solve the problem of providing a plant cultivation agent that can be used as a spray agent with low environmental impact and high safety, the applicant of the present application disclosed in Patent Document 1 that a plant cultivation agent that contains cellulose nanofibers and that can be used directly or indirectly on plants. A plant cultivation agent which is added, sprinkled or sprayed and whose insecticidal active ingredient is cellulose nanofibers is disclosed.

また、本願出願人は特許文献2に、家畜等の生育環境を容易に整えることができ、かつ、従業員の労働環境を改善するという課題を解決するために、1~100μmのマイクロ繊維或いは、3~1000nmのナノ繊維の繊維幅を有する繊維を含有する畜舎用環境改善養分散液を開示した。 In addition, the applicant of the present application discloses in Patent Document 2 that in order to solve the problem of easily preparing the breeding environment for livestock etc. and improving the working environment of employees, the applicant has introduced microfibers of 1 to 100 μm or An environment-improving nutrient dispersion for livestock housing containing fibers having a nanofiber fiber width of 3 to 1000 nm is disclosed.

さらに、特許文献3には、施肥装置を詰まらせない均一な施肥、および液体肥料と混合する前の事前希釈または事前スラリーを必要としない施肥として、(a)農業用生物活性物質、殺菌剤、殺虫剤、除草剤、および/または植物成長調節剤。(b)フィブリルまたはミクロフィブリルまたはナノフィブリル構造化剤、および(c)補助界面活性剤を含む組成物が開示されている。しかしながら、具体的に農場や畜舎等に散布した等という実施例は記載されていない。 Furthermore, Patent Document 3 describes (a) an agricultural biologically active substance, a fungicide, Pesticides, herbicides, and/or plant growth regulators. Compositions are disclosed that include (b) a fibril or microfibril or nanofibril structuring agent, and (c) a cosurfactant. However, there is no mention of any specific examples of spraying on farms, livestock barns, etc.

特許6639036号Patent No. 6639036 特許6867613号Patent No. 6867613 特表2020-531420号公報Special Publication No. 2020-531420

耕作規模や畜産農業の規模によるところもあるが、農業分野全体においては、一般的に、比較的多くの量の散布液を耕作地や畜舎等に散布・噴霧する。そして、この散布液の量に比例して、散布・噴霧に要する時間は、長くなるのが通常である。 Although it depends on the scale of cultivation and livestock farming, in the agricultural field as a whole, a relatively large amount of spray liquid is generally sprayed on cultivated land, livestock sheds, etc. The time required for dispersion/spraying usually increases in proportion to the amount of the spray liquid.

一方、セルロースナノファイバーを初めとする微細状繊維等は、アスペクト比の高い繊維状の物質であるため、微細状繊維を含有する散布液の散布時間の経過とともに、微細状繊維が散布装置のノズル等に詰まってしまい、持続的に散布を行うことができないと考えられる。そのため、繊維幅1~100μmのマイクロ繊維の微細状繊維を含有する散布液を散布する場合には特に、ノズル等の分解洗浄を頻繁に行う必要があり、効率的に散布液を散布・噴霧することができないという問題が想定される。 On the other hand, fine fibers such as cellulose nanofibers are fibrous substances with a high aspect ratio. It is thought that the spray will become clogged with the water, making it impossible to spray continuously. Therefore, especially when spraying a spray solution containing microfibers with a fiber width of 1 to 100 μm, it is necessary to frequently disassemble and clean the nozzle, etc., in order to efficiently spread and spray the spray solution. The problem is that it cannot be done.

また、セルロースナノファイバーを初めとする微細状繊維が各種溶媒中に存在する場合には、微細状繊維同士が相互に凝集してしまい、散布装置内において、微細状繊維が沈降し、偏在化してしまう可能性が高い。そのため、微細状繊維を含有する散布液の濃度を均一に保ったまま、散布液を散布・噴霧することができないという問題が想定される。 In addition, when fine fibers such as cellulose nanofibers are present in various solvents, the fine fibers coagulate with each other, causing them to settle and become unevenly distributed in the spraying device. There is a high possibility that it will go away. Therefore, a problem can be assumed that it is not possible to spread/spray the spray liquid containing fine fibers while keeping the concentration of the spray liquid uniform.

本発明は、以上の問題に鑑み、耕種農業や畜産農業等の農業分野全般の現場において、多量の微細状繊維を含む散布液を効率的に行うことができる散布装置及び微細状繊維を含む散布液の散布装置を用いた散布方法を提供することを目的とする。 In view of the above-mentioned problems, the present invention provides a spraying device and a spraying device capable of efficiently distributing a spray solution containing a large amount of fine fibers in general agricultural fields such as cultivation agriculture and livestock farming. The object of the present invention is to provide a spraying method using a liquid spraying device.

本発明者等は、上記目的を達成するために鋭意検討を行った結果、微細状繊維を相互に凝集させないようにするために、散布液を流動状態とすることにより、前記課題を解決できることを見出し、本発明を完成するに至ったものである。 As a result of intensive studies to achieve the above object, the present inventors have found that the above problem can be solved by making the spray liquid in a fluid state in order to prevent the fine fibers from coagulating with each other. This is the heading that led to the completion of the present invention.

すなわち、本発明の微細状繊維を含む散布液の散布装置は、少なくとも、循環戻り口と散布液投入口を備える貯蔵タンクと、噴霧ノズルと、循環口と、吐出口と、吸水口とを備える動力噴霧器と、前記循環口に一端が接続し、他端を前記散布液投入口に投入する循環配管と、前記吐出口に一端が接続し、他端が前記噴霧ノズルに接続した吐出配管と、前記吸水口に一端が接続し、他端が前記貯蔵タンクに接続した吸水配管と、前記貯蔵タンクに接続した吸水配管の吸込口に、前記貯蔵タンクの底面と前記吸込口との距離を維持するための部材とを備える。 That is, the spraying device for a spraying liquid containing fine fibers of the present invention includes at least a storage tank having a circulation return port and a spraying liquid input port, a spray nozzle, a circulation port, a discharge port, and a water intake port. a power sprayer, a circulation pipe whose one end is connected to the circulation port and whose other end is input to the spray liquid input port, and a discharge pipe whose one end is connected to the discharge port and whose other end is connected to the spray nozzle; A water suction pipe connected at one end to the water suction port and the other end connected to the storage tank, and a suction port of the water suction pipe connected to the storage tank, maintaining a distance between the bottom surface of the storage tank and the suction port. and a member for.

また、微細状繊維を含む散布液の散布装置を用いた散布方法は、微細状繊維を含有する分散体前記分散体の容量の5~10倍の水で希釈して第一の希釈体を調製する第一の希釈工程と、第一の希釈体を水で希釈して所定の濃度の微細状繊維を含有する散布液とする第二の希釈工程とを有する混合工程と、前記微細状繊維を含有する散布液を、前記貯蔵タンクと、前記循環配管と、動力噴霧器とを利用して、循環させる循環工程と、前記噴霧ノズルを利用して、所定の場所へ散布する散布工程とを備える。 In addition, in a method of spraying a spray liquid containing fine fibers using a spraying device, a first diluted body is prepared by diluting the dispersion containing fine fibers with water 5 to 10 times the volume of the dispersion. a mixing step having a first dilution step of diluting the first diluent with water to obtain a spray liquid containing fine fibers at a predetermined concentration; The method includes a circulation step of circulating the contained spray liquid using the storage tank, the circulation piping, and a power sprayer, and a spraying step of spraying the spray liquid to a predetermined location using the spray nozzle.

本発明により、耕種農業や畜産農業等の農業分野全般の現場において、多量の微細状繊維の散布を効率的に行うことができる散布装置及び散布装置を用いた散布方法が提供される。 The present invention provides a spraying device and a spraying method using the spraying device that can efficiently spray a large amount of fine fibers in general agricultural fields such as arable farming and livestock farming.

本願発明の一実施の形態の微細状繊維を含む散布液の散布装置の概念図である。FIG. 1 is a conceptual diagram of a spraying device for a spraying liquid containing fine fibers according to an embodiment of the present invention. 螺旋状の溝を有する中子を備えた回転機構を有する噴霧ノズルである。This is a spray nozzle that has a rotating mechanism that includes a core that has a spiral groove. 外気取り込み口を備えた泡状ノズルである。It is a foam nozzle with an outside air intake port. 本願発明の一実施の形態の貯蔵タンクの底面と吸水口との距離を維持するための部材の一実施形態である。This is an embodiment of a member for maintaining the distance between the bottom surface of a storage tank and a water intake port according to an embodiment of the present invention. 本願発明の一実施の形態の貯蔵タンクの底面と吸水口との距離を維持するための部材の他の一実施形態である。This is another embodiment of the member for maintaining the distance between the bottom surface of the storage tank and the water intake port according to the embodiment of the present invention. 微細状繊維を含有する散布液の一部の様子を示したものである。This figure shows a part of the spray liquid containing fine fibers. 微細状繊維を含有する散布液を散布する様子を示したものである。This figure shows how a spray liquid containing fine fibers is sprayed. 比較例1において調製した液の一部の様子を示したものである。This figure shows a part of the liquid prepared in Comparative Example 1.

次に、本発明の実施の形態を詳しく説明する。ただし、以下の実施形態は、発明の理解を助けるためのものであり、本発明を限定するものではない。 Next, embodiments of the present invention will be described in detail. However, the following embodiments are for helping understanding the invention, and are not intended to limit the invention.

(用語の定義)
本発明に係る微細状繊維との用語は、繊維幅が1~100μm、繊維長が0.1~10mmであるマイクロ繊維と繊維幅が3~1000nm、繊維長が1~200μmであるナノ繊維とを含む概念のものである。
また、その由来成分及びその製造方法等は、特許第6867613号公報に記載の微細状繊維の製造方法や特許第6704551号公報に記載の天然高分子としてセルロースを用いたセルロースナノファイバー及びセルロースナノクリスタル水溶液の調製方法や両公報に記載の他の原料等を由来成分とする微細状繊維の製造方法を参照することができる。
微細状繊維を含む分散体との用語は、微細状繊維と溶媒とからなる微細状繊維を含有する分散液のみならず、粉末状の微細状繊維を、溶媒を用いて分散させた微細状繊維を含有する分散液を含む概念のものである。
(Definition of terms)
The term "fine fiber" according to the present invention refers to microfibers with a fiber width of 1 to 100 μm and fiber length of 0.1 to 10 mm, and nanofibers with a fiber width of 3 to 1000 nm and fiber length of 1 to 200 μm. It is a concept that includes.
In addition, its derived components and its manufacturing method are described in the method for manufacturing fine fibers described in Japanese Patent No. 6867613, and cellulose nanofibers and cellulose nanocrystals using cellulose as a natural polymer described in Japanese Patent No. 6704551. Reference can be made to the method for preparing an aqueous solution and the method for producing fine fibers using other raw materials as derived components described in both publications.
The term "dispersion containing fine fibers" refers not only to a dispersion containing fine fibers consisting of fine fibers and a solvent, but also to fine fibers in which powdered fine fibers are dispersed using a solvent. The concept includes a dispersion containing .

(微細状繊維を含む散布液の散布装置)
まず、図1を参照して、本発明の実施の形態に係る微細状繊維を含む散布液の散布装置1を説明する。
本発明の散布装置1は、循環戻り口3と散布液投入口4を備える貯蔵タンク2と、噴霧ノズル5と、循環口6と、吐出口7と、吸水口8とを備える動力噴霧器9と、前記循環口6に一端が接続し、他端を前記循環戻り口3に接続する循環配管10と、前記吐出口7に一端が接続し、他端が前記噴霧ノズル5に接続した吐出配管11と、前記吸水口8に一端が接続し、他端が前記貯蔵タンク2に接続した吸水配管12と、前記貯蔵タンク2に接続した吸水配管12の吸込口13に、前記貯蔵タンク2の底面と前記吸込口13との距離を維持するための部材14とを備える。
(Spraying device for spraying liquid containing fine fibers)
First, referring to FIG. 1, a spraying device 1 for spraying liquid containing fine fibers according to an embodiment of the present invention will be described.
The spraying device 1 of the present invention includes a storage tank 2 having a circulation return port 3 and a spray liquid input port 4, a power sprayer 9 including a spray nozzle 5, a circulation port 6, a discharge port 7, and a water intake port 8. , a circulation pipe 10 whose one end is connected to the circulation port 6 and the other end to the circulation return port 3; and a discharge pipe 11 whose one end is connected to the discharge port 7 and the other end is connected to the spray nozzle 5. and a water suction pipe 12 whose one end is connected to the water suction port 8 and the other end is connected to the storage tank 2, and the bottom surface of the storage tank 2 is connected to the suction port 13 of the water suction pipe 12 connected to the storage tank 2. A member 14 for maintaining a distance from the suction port 13 is provided.

貯蔵タンク2は、少なくとも、循環戻り口3と、微細状繊維を含む散布液を供給するための散布液投入口4、動力噴霧器の吸水口8へ接続するための接続部15を備える。また、前記循環戻り口は、前記散布液投入口4に循環配管10が接続でき更にホース等を用いて吸込口13に繋ぎ込むようにしてもよい。
また、貯蔵タンク2の底面は、前記部材14が低い位置となるように傾斜をつけてもよく、その場合は残液量を減らすことができる。
さらに、貯蔵タンク2には加温機構、冷却機構、加圧機構及び攪拌機構等を備えていてもよい。
The storage tank 2 comprises at least a circulation return port 3, a spray liquid inlet 4 for supplying a spray liquid containing fine fibers, and a connection 15 for connection to a water intake 8 of a power sprayer. Further, the circulation return port may be connected to the circulation pipe 10 to the spray liquid input port 4, and further may be connected to the suction port 13 using a hose or the like.
Further, the bottom surface of the storage tank 2 may be sloped so that the member 14 is at a lower position, in which case the amount of remaining liquid can be reduced.
Furthermore, the storage tank 2 may be equipped with a heating mechanism, a cooling mechanism, a pressurizing mechanism, a stirring mechanism, and the like.

噴霧ノズル5としては特に制限されず市販されている一般的なノズルを用いることができるが、特に最適なノズル形状について図2及び図3を用いて説明する。
図2は、螺旋状の溝16を有する中子17を備えた回転機構(旋回機構)を有する噴霧ノズルである。回転機構(旋回機構)とは、流体の移動を利用して流体に回転流を生じさせる仕組みを有する機構のことをいう。この回転流により繊維の沈降を防ぎ、凝集繊維による閉塞の可能性を低減できる。動力噴霧機などの外部動力により回転流を促しても良いが、流動形状のみで回転流が生じて沈降を抑制することができるとことができて省エネルギーや故障トラブル面からみても更に良い。
図3は、外気取り込み口18を備えた泡状ノズルである。泡状ノズルとは、気泡相と液相を生じるノズルのことをいう。泡状ノズルを用いることによって、微細状繊維は、気泡相の外表面に吸着するように膜状に広がり、気泡相を囲むことで均一に分散する作用が生じており、結果として繊維の凝集・沈降を防ぎ均一な噴霧状態とし良好な結果を生じている。このような泡状ノズルでは、外気を効率的に取り込むためには内圧が外圧より低いことが必要条件となる。そのため外気取り込み口18の前流路と後流路に散布液の通過する細孔24と25を設けてあり、その細孔の大きさが24より25の方が大きいことで18から外気を取り込む吸引力が生じる。
Although the spray nozzle 5 is not particularly limited and can be any commercially available general nozzle, a particularly optimal nozzle shape will be described with reference to FIGS. 2 and 3.
FIG. 2 shows a spray nozzle having a rotating mechanism (swivel mechanism) including a core 17 having a spiral groove 16. A rotating mechanism (swivel mechanism) refers to a mechanism that uses the movement of fluid to generate a rotational flow in the fluid. This rotating flow prevents the fibers from settling and reduces the possibility of clogging due to aggregated fibers. Although the rotational flow may be promoted by external power such as a power sprayer, it is possible to generate a rotational flow and suppress sedimentation by changing the flow shape alone, which is even better from the viewpoint of energy saving and failure trouble.
FIG. 3 shows a foam nozzle with an outside air intake port 18. A foam nozzle refers to a nozzle that generates a bubble phase and a liquid phase. By using a foam nozzle, the fine fibers spread out like a film so as to be adsorbed to the outer surface of the foam phase, and by surrounding the foam phase, a uniform dispersion effect occurs, resulting in fiber aggregation and It prevents sedimentation and creates a uniform spray, giving good results. In such a foam nozzle, in order to efficiently take in outside air, it is necessary that the internal pressure be lower than the external pressure. For this reason, pores 24 and 25 through which the spray liquid passes are provided in the front flow path and the rear flow path of the outside air intake port 18, and the size of the pores 25 is larger than 24, so that outside air can be taken in from the outside air intake port 18. A suction force is generated.

循環口6と、吐出口7と、吸水口8とを備える動力噴霧器9は、ガソリンや電気などの動力源を用いて、液体の農薬等を散布する機械として用いられているものであれば、特に制限なく用いることができる。具体的には、水中ポンプ、電池式噴霧器等を例示することができる。 The power sprayer 9, which includes a circulation port 6, a discharge port 7, and a water intake port 8, can be used as a machine for spraying liquid pesticides using a power source such as gasoline or electricity. It can be used without particular restrictions. Specifically, submersible pumps, battery-powered sprayers, etc. can be exemplified.

動力噴霧器9の循環口6に一端が接続し、他端を前記循環戻し口3と接続した循環配管10、吐出口7に一端が接続し、他端が前記噴霧ノズル5に接続した吐出配管11及び吸水口8に一端が接続し、他端が前記貯蔵タンク2に接続した吸水配管8としては、この種の配管として用いられているものであれば、特に制限なく使用することができる。また、配管とは液体を移送する手段をいい、その目的に合致するものであれば特に制限なく、例えばステンレスパイプ、塩ビ配管、ビニルホースなどが利用できる。 A circulation pipe 10 has one end connected to the circulation port 6 of the power sprayer 9 and the other end connected to the circulation return port 3, and a discharge pipe 11 has one end connected to the discharge port 7 and the other end connected to the spray nozzle 5. The water suction pipe 8, which has one end connected to the water suction port 8 and the other end connected to the storage tank 2, can be used without any particular restriction as long as it is used as this type of piping. Further, piping refers to a means for transferring liquid, and there is no particular restriction as long as it meets the purpose, and for example, stainless steel pipes, PVC piping, vinyl hoses, etc. can be used.

前記循環戻り口3を介して、前記動力噴霧器9と循環配管10を用いて、貯蔵タンク2から送液した散布液を循環戻し口3から、散布液を貯蔵タンク2に再度投入することによって、散布液を流動状態とすることができる。このことを散布液の循環という。 By using the power sprayer 9 and circulation piping 10 to feed the spray liquid from the storage tank 2 via the circulation return port 3, the spray liquid is again introduced into the storage tank 2 from the circulation return port 3. The spray liquid can be in a fluid state. This is called circulation of the spray liquid.

貯蔵タンク2に接続した吸水配管12の吸込口13に、前記貯蔵タンク2の底面と前記吸込口13との距離を維持するための部材14は、吸水配管12の吸込口13が、貯蔵タンク2の底面に接しないようにするために、用いるものである。係る目的を達成できる形状であれば、部材14の形状については特には制限されないが、以下に、具体的な部材の形状についていくつか例を提示する。 A member 14 for maintaining the distance between the bottom surface of the storage tank 2 and the suction port 13 is attached to the suction port 13 of the water suction pipe 12 connected to the storage tank 2. This is used to prevent contact with the bottom surface of the The shape of the member 14 is not particularly limited as long as it can achieve the above purpose, but some examples of specific member shapes will be presented below.

図4を用いて、貯蔵タンクの底面と吸水口との距離を維持するための部材の一実施形態について説明する。本実施形態における部材14は、既存のストレーナー19に錘20を複数個接続したものである。このようにすることによって、物理的にストレーナー19が底面に直接接触しないようにし、貯蔵タンクの底面21と吸水口13との距離を維持することができる。
図5を用いて、貯蔵タンクの底面と吸水口との距離を維持するための部材の他の一実施形態について説明する。本実施形態における部材14は、吸水口13と接続部を有する板22に、錘20を複数接続し、錘間の領域23に、目開き300μm以上の格子状のメッシュ或いは、目開き200μm以上のスリット状のメッシュを張る。このようにすることによって、吸い込み部の面積を広くとり、吸い込み流速を下げることで、底面に存在する可能性のある砂等の重量異物を吸い上げないようにすることができる。
また、図示しないが、貯蔵タンクの底面と吸水口との距離を維持するための部材の他の一実施形態としては、貯蔵タンクの底部に堆積存在する砂などの重量異物を直接吸い上げないように、底部から距離を維持するために、例えば、底面1cm程度上の位置を最下部とする開口部10cm程度のフランジをタンク2の側面に設けて、(つまり、前記フランジが貯蔵タンクの底面から1cm程度嵩上げした位置に設ける。)吸水配管を接続する、或いは、動力噴霧器を直接繋いで、これを吸水口とする等の形態がある。
An embodiment of a member for maintaining the distance between the bottom surface of the storage tank and the water intake port will be described using FIG. 4. The member 14 in this embodiment is an existing strainer 19 with a plurality of weights 20 connected thereto. By doing so, the strainer 19 can be physically prevented from coming into direct contact with the bottom surface, and the distance between the bottom surface 21 of the storage tank and the water intake port 13 can be maintained.
Another embodiment of the member for maintaining the distance between the bottom surface of the storage tank and the water intake port will be described using FIG. 5. In the member 14 of this embodiment, a plurality of weights 20 are connected to a plate 22 having a water inlet 13 and a connection part, and a region 23 between the weights is provided with a grid-like mesh with an opening of 300 μm or more or a grid-like mesh with an opening of 200 μm or more. Spread a slit-shaped mesh. By doing so, by increasing the area of the suction part and lowering the suction flow velocity, it is possible to prevent heavy foreign matter such as sand that may be present on the bottom surface from being sucked up.
Although not shown, another embodiment of a member for maintaining the distance between the bottom of the storage tank and the water intake port is a member that prevents heavy foreign matter such as sand that is accumulated at the bottom of the storage tank from being directly sucked up. In order to maintain the distance from the bottom, for example, a flange with an opening of about 10 cm is provided on the side of the tank 2, and the lowest opening is about 1 cm above the bottom (that is, the flange is 1 cm from the bottom of the storage tank). (Provided at a somewhat elevated position.) There are several ways to connect the water suction pipe, or to directly connect a power sprayer and use this as the water suction port.

本発明に係る散布装置においては、微細状繊維を含有する散布液の流路のいずれかの箇所に、用いる微細繊維の繊維長さに応じて目開き300μm以上の格子状のメッシュ或いは、用いる微細繊維の繊維幅に応じて目開き200μm以上のスリット状のメッシュを使用するようにするとよい。尚、スリット状の方がより繊維を通過させ易くし、砂などの重量異物を容易に除去できる。使用するノズルの開口径によりスリット幅を細くし、これを通過できるサイズの微細繊維を選定しても良い。但し微細状繊維のサイズを細かくすることは薬液コスト増に繋がることもあるので用途に応じて選定する必要がある。
一方、特に畜産用途など0.9mm以上のノズル径利用の場合、本発明に係る散布装置においては、目開き300μm未満の格子状のメッシュ或いは目開き200μm未満のスリット状のメッシュは、使用しないようにするとより安価な薬液でも効率的に噴霧できてよい。目開き300μm未満の格子状のメッシュ或いは目開き200μm未満のスリットを用いた場合には、微細状繊維が前記メッシュ或いはスリット状のメッシュに詰まってしまい、散布を継続して行うことができないからである。
ここで、本願発明における微細状繊維を含有する散布液の散布装置が、貯蔵タンクの底面と吸水口との距離を維持するための部材や前記メッシュを備えることの必要性は以下の通りである。
耕種農業や畜産農業等の現場においては、収穫量の増大や畜舎の環境を改善する等の用途のため通常200~10000Lの各種有効成分等を含有する散布液を連続的に散布している。また、散布装置や貯蔵タンクを半屋外や屋外に保管することもある。このような状況を鑑みると、貯蔵タンクの中に砂、小石等の重量異物或いはビニール等の軽量異物が存在する必然性が高くなるといえる。
また、前記用途のために、通常散布する散布液には、繊維幅が1~100μmのマイクロ繊維や繊維幅が3~1000nmのナノ繊維の微細状繊維を意図して配合することはない。
以上のことから、貯蔵タンク中に重量異物が存在する可能性の高い散布装置において、前記の幅の微細状繊維を含有する散布液を200~10000L散布するために必要な散布装置が求められている。すわなち、貯蔵タンクの底面と吸水口との距離を維持するための部材は、貯蔵タンクの底面に存在する砂、小石等の重量異物、およびビニール等の大きな軽量異物を吸い込まないようにするためのものでもある。仮に、重量異物等を吸入口に、吸い込んでしまった場合には、ここに、微細状繊維が堆積したりノズル先端を閉塞したり設備内面に損傷を与えたりするからである。ビニール等の大きな軽量異物の場合はノズル手前に貼り付いて閉塞させることがある。
また、前記本発明で用いる目開き300μm以上の格子状のメッシュ或いは、用いる微細繊維の繊維幅に応じて目開き200μm以上のスリット状のメッシュよりも、細かいものを使用した場合には、これらに付着・堆積・閉塞してしまい、散布液を散布することができなくなるためである。
In the spraying device according to the present invention, depending on the fiber length of the fine fibers used, a lattice-like mesh with an opening of 300 μm or more is installed at any point in the flow path of the spray liquid containing the fine fibers. It is preferable to use a slit-like mesh with an opening of 200 μm or more depending on the fiber width of the fibers. Note that a slit shape allows fibers to pass through more easily, and heavy foreign substances such as sand can be easily removed. The slit width may be narrowed depending on the opening diameter of the nozzle used, and fine fibers of a size that can pass through the slit may be selected. However, reducing the size of the fine fibers may lead to an increase in the cost of the chemical solution, so it is necessary to select it depending on the application.
On the other hand, especially when using a nozzle diameter of 0.9 mm or more, such as in livestock farming, it is recommended not to use a grid-like mesh with an opening of less than 300 μm or a slit-like mesh with an opening of less than 200 μm in the spraying device according to the present invention. This allows even cheaper chemical solutions to be sprayed efficiently. If a lattice-like mesh with an opening of less than 300 μm or a slit with an opening of less than 200 μm is used, the fine fibers will clog the mesh or slit-like mesh, making it impossible to continue spreading. be.
Here, the necessity for the spraying device for spraying liquid containing fine fibers in the present invention to be provided with a member for maintaining the distance between the bottom of the storage tank and the water intake port and the mesh is as follows. .
In fields such as arable farming and livestock farming, 200 to 10,000 L of spray liquid containing various active ingredients is normally sprayed continuously for purposes such as increasing yields and improving the environment of livestock barns. Additionally, spraying equipment and storage tanks may be stored semi-outdoors or outdoors. In view of this situation, it can be said that there is a high probability that heavy foreign objects such as sand and pebbles or lightweight foreign objects such as vinyl will exist in the storage tank.
Further, for the above-mentioned applications, fine fibers such as microfibers with a fiber width of 1 to 100 μm or nanofibers with a fiber width of 3 to 1000 nm are not intentionally blended into the spray liquid that is normally sprayed.
Based on the above, there is a demand for a spraying device that is necessary to spray 200 to 10,000 L of a spray liquid containing fine fibers of the above width in a spraying device where heavy foreign matter is likely to be present in the storage tank. There is. In other words, the member for maintaining the distance between the bottom of the storage tank and the water intake port is designed to prevent heavy foreign objects such as sand and pebbles from being sucked into the bottom of the storage tank, as well as large lightweight foreign objects such as vinyl. It is also for. This is because, if a heavy foreign object or the like is sucked into the suction port, fine fibers may accumulate there, clog the nozzle tip, or damage the inside of the equipment. Large lightweight foreign objects such as vinyl may stick to the front of the nozzle and block it.
Furthermore, if a mesh that is finer than the lattice-like mesh with an opening of 300 μm or more used in the present invention or the slit-like mesh with an opening of 200 μm or more depending on the fiber width of the fine fibers used, This is because the particles adhere, accumulate, and become clogged, making it impossible to spray the spray liquid.

(微細状繊維を含む散布液の散布方法)
次に、本発明に係る微細状繊維を含む散布液散布装置を用いた微細状繊維を含む散布液の散布方法について説明する。
通常、耕作規模や畜産農業において、微細状繊維を含有する散布液中の微細状繊維の濃度は、0.001~0.5%程度である。また、通常、流通する微細状繊維を含む分散液の微細状繊維の濃度は、0.1~15%の範囲のものであり、多くは、1~3%程度の範囲のものである。したがって、微細状繊維を含有する散布液とするためには、前記分散液を希釈する必要がある。また、粉末状の微細状繊維を用いた場合も、粉末状の微細状繊維に水等の溶媒を加えて、微細状繊維を含有する散布液を調製する必要がある。
(Method of spraying a spray liquid containing fine fibers)
Next, a method for spraying a spray liquid containing fine fibers using the spray liquid spraying device containing fine fibers according to the present invention will be described.
Normally, in cultivation scales and livestock farming, the concentration of fine fibers in the spray liquid containing fine fibers is about 0.001 to 0.5%. Further, the concentration of fine fibers in the distributed dispersion liquid containing fine fibers is usually in the range of 0.1 to 15%, and often in the range of about 1 to 3%. Therefore, in order to obtain a spray liquid containing fine fibers, it is necessary to dilute the dispersion liquid. Furthermore, even when powdered fine fibers are used, it is necessary to add a solvent such as water to the powdered fine fibers to prepare a spray liquid containing the fine fibers.

(混合工程)
本発明の混合工程は、混合工程(A)又は混合工程(B)のいずれかを選択することができる。
混合工程(A)は、微細状繊維を含有する分散体を、この分散体の容量の5~10倍の水で希釈して、第一の希釈体を調製する第一の希釈工程と、第一の希釈体を水で希釈して所定の濃度の微細状繊維を含有する散布液とする第二の希釈工程とを有する工程である。
より具体的に、混合工程(A)の一例を説明すると、微細状繊維を含有する分散体の容量が200Lである場合には、これを1000~2000Lの水を用いて希釈し、次いで、所望の濃度となるように、水で希釈して微細状繊維を含有する散布液とする。なお、このときの希釈方法は特に制限されず、前記水の一部を貯蔵タンクに貯水し、次いで、微細状繊維を含有する分散体を投入し、混合撹拌し、微細状繊維同士の絡み合いをほぐしながら、残りの水を投入する等の方法を用いてもよい。
(Mixing process)
As the mixing step of the present invention, either the mixing step (A) or the mixing step (B) can be selected.
The mixing step (A) includes a first dilution step in which a dispersion containing fine fibers is diluted with water of 5 to 10 times the volume of this dispersion to prepare a first diluted product; This process includes a second dilution step in which the first diluent is diluted with water to obtain a spray liquid containing fine fibers at a predetermined concentration.
More specifically, to explain an example of the mixing step (A), when the volume of the dispersion containing fine fibers is 200 L, this is diluted with 1000 to 2000 L of water, and then the desired amount is The solution is diluted with water to give a concentration of . Note that the dilution method at this time is not particularly limited; a portion of the water is stored in a storage tank, and then a dispersion containing fine fibers is added and mixed and stirred to prevent entanglement of the fine fibers. You may also use a method such as adding the remaining water while loosening.

混合工程(B)は、微細状繊維を含有する分散体を水で希釈して0.1%以上の濃度の第一の希釈体を調製する第一の希釈工程と、第一の希釈体を、第一の希釈体の等倍以上の水で希釈して、所定の濃度の微細状繊維を含有する散布液とする第二の希釈工程とを有する工程である。
より具体的に、混合工程(B)の一例を説明すると、微細状繊維を含有する分散体の濃度が1%である場合には、これを、水を用いて0.1%以上の濃度にし、次いで、第一の希釈体の容量と等倍以上の水で希釈して、所定の濃度の微細状繊維を含有する散布液とする。なお、このときの希釈方法は特に制限されず、前記水の一部を貯蔵タンクに貯水し、次いで、微細状繊維を含有する分散体を投入し、混合撹拌し、微細状繊維同士の絡み合いをほぐしながら、残りの水を投入する等の方法を用いてもよい。
The mixing step (B) includes a first dilution step in which a dispersion containing fine fibers is diluted with water to prepare a first diluted product having a concentration of 0.1% or more; , and a second dilution step of diluting the first diluent with water in an amount equal to or larger than that of the first diluent to obtain a spray liquid containing fine fibers at a predetermined concentration.
More specifically, to explain an example of the mixing step (B), when the concentration of the dispersion containing fine fibers is 1%, this is made to have a concentration of 0.1% or more using water. Then, the first diluent is diluted with water equal to or larger than the volume of the first diluent to obtain a spray liquid containing fine fibers at a predetermined concentration. Note that the dilution method at this time is not particularly limited; a portion of the water is stored in a storage tank, and then a dispersion containing fine fibers is added and mixed and stirred to prevent entanglement of the fine fibers. You may also use a method such as adding the remaining water while loosening.

このような混合工程とすることで、第一の希釈工程において、微細状繊維にシェアを付与して、第二の希釈工程を実施する前に、微細状繊維同士の絡み合いをほぐすことができる。また、微細状繊維を含む散布液中の微細状繊維同士が凝集してしまうことを防ぐことができる。一方、本発明に係る混合工程を行わないで、微細状繊維を含む分散体に単に水を加えて所定の濃度とすると、微細状繊維同士が凝集してしまい、微細状繊維を含む散布することが困難となる。
なお、貯蔵タンク2に加温機構、冷却機構、加圧機構及び攪拌機構等を備えた場合には、適宜、加温、冷却、加圧、攪拌等を行ってもよい。
By performing such a mixing step, it is possible to impart shear to the fine fibers in the first dilution step and loosen the entanglements between the fine fibers before implementing the second dilution step. Furthermore, it is possible to prevent fine fibers in the spray liquid containing fine fibers from aggregating with each other. On the other hand, if water is simply added to a dispersion containing fine fibers to achieve a predetermined concentration without performing the mixing process according to the present invention, the fine fibers will aggregate with each other, making it difficult to disperse the fine fibers. becomes difficult.
In addition, when the storage tank 2 is equipped with a heating mechanism, a cooling mechanism, a pressurizing mechanism, a stirring mechanism, etc., heating, cooling, pressurizing, stirring, etc. may be performed as appropriate.

(循環工程)
循環工程は、微細状繊維を含有する散布液を、貯蔵タンクと、循環配管と、動力噴霧器とを利用して、循環戻り口を介して、貯蔵タンクと循環配管との間で、微細状繊維を含む分散体や微細状繊維を含有する散布液を循環させる工程である。このような工程とすることで、動力噴霧器を使用して、貯蔵タンク中の散布液を常に流動状態とするように貯蔵タンクに散布液を戻すことができる。したがって、混合工程と同様に、微細状繊維を含む散布液中の微細状繊維同士が凝集したまま存在してしまうことを防ぐことができ、また、貯蔵タンク中の微細状繊維の濃度差をも防ぐことができる。
また、本発明の循環工程は、混合工程における第一の希釈工程及び第二の希釈工程において、本工程を行うことにより、更に良好な分散状態を得ることができる。
(circulation process)
The circulation process uses a storage tank, circulation piping, and a power sprayer to transfer a spray liquid containing fine fibers between the storage tank and circulation piping through a circulation return port. This is a process of circulating a dispersion containing fine fibers and a spray solution containing fine fibers. With such a process, the power sprayer can be used to return the spray liquid to the storage tank so that the spray liquid in the storage tank is always in a fluid state. Therefore, as in the mixing process, it is possible to prevent fine fibers in the spray liquid containing fine fibers from remaining agglomerated together, and also to reduce the concentration difference of fine fibers in the storage tank. It can be prevented.
Further, in the circulation step of the present invention, by performing this step in the first dilution step and the second dilution step in the mixing step, an even better dispersion state can be obtained.

(散布工程)
散布工程は、噴霧ノズルを利用して、所定の場所へ微細状繊維を含む散布液を散布する散布工程である。
動力噴霧器の吸水量は、1~75L/min、圧力は、1MPa以上、好ましくは、3MPa以上とすればよい。
一般的に、CNF分散液は、チキソ性を有する分散液であることが知られており、シェアが低下すれば固体状を呈し、シェアが高まれば液状になる。内径20mm(半径10mm)の配管内部にCNFを流して外付けの電磁流量計で流量を測定する場合に1分間に5L以下の流量になると流量計のカウントが難しくなる。この流速以下で固体の性質を呈し始めるため配管外側に繊維が沈降堆積始めるためである。この閾値の流速は内径と流量から下のように計算することができ、この流速値0.27 m / s以上で常に液を動かし続けることにより、良好な散布性を維持することができる。使用設備の配管サイズやノズル口径などは用途により異なるが、給水量、流量をこの流速を維持できる範囲で自由に設定することで解決することができる。
5 L/min × 0.001m3/L÷60 s / min ÷ ( 0.01 m × 0.01 m × π) ≒ 0.27 m/s
(Spraying process)
The spraying process is a spraying process in which a spray liquid containing fine fibers is sprayed onto a predetermined location using a spray nozzle.
The water absorption amount of the power sprayer may be 1 to 75 L/min, and the pressure may be 1 MPa or more, preferably 3 MPa or more.
Generally, a CNF dispersion liquid is known to be a dispersion liquid having thixotropic properties, and when the shear decreases, it becomes solid, and when the shear increases, it becomes liquid. When flowing CNF inside a pipe with an inner diameter of 20 mm (radius 10 mm) and measuring the flow rate with an external electromagnetic flow meter, if the flow rate is less than 5 L per minute, it becomes difficult to count with the flow meter. This is because below this flow rate, the fibers begin to exhibit solid properties and begin to settle and accumulate on the outside of the pipe. This threshold flow velocity can be calculated from the inner diameter and flow rate as shown below, and by constantly moving the liquid at this flow velocity value of 0.27 m/s or more, good dispersion properties can be maintained. Although the piping size and nozzle diameter of the equipment used will vary depending on the application, problems can be solved by freely setting the water supply amount and flow rate within a range that maintains the flow rate.
5 L/min × 0.001m3/L÷60 s / min ÷ (0.01 m × 0.01 m × π) ≒ 0.27 m/s

(除去工程)
除去工程は、前記混合工程、循環工程、散布工程を通じて、貯蔵タンク側の吸水配管先端につけた部材を利用して貯蔵タンクの中に砂、小石等の重量異物或いはビニール等の軽量異物を除去する工程である。本発明において用いられる部材は、底面と吸入口との距離を維持するためのものであるから、貯蔵タンクの底面に存在する可能性のある砂等の重量異物を吸い上げないようにすることができる。
(Removal process)
In the removal process, through the mixing process, circulation process, and spraying process, heavy foreign substances such as sand and pebbles, or light foreign substances such as vinyl are removed from the storage tank using a member attached to the tip of the water absorption pipe on the storage tank side. It is a process. Since the member used in the present invention is for maintaining the distance between the bottom surface and the suction port, it is possible to prevent heavy foreign objects such as sand that may be present on the bottom surface of the storage tank from being sucked up. .

以下、実施例に基づき本発明を説明するが、本発明はこれらの実施例に限定されるものではない。 The present invention will be described below based on Examples, but the present invention is not limited to these Examples.

(実施例1)
図1に示す微細状繊維を含む散布液の散布装置と基本構成が同じ装置及び図2に示す部材と基本構成が同じ部材を用いて、以下の工程により、散布液を作成し、これを養鶏場において散布した。
まず、貯蔵タンクに、CNF分散体(CNF濃度2%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)10Lと水を100L加えて第一の希釈体とした。次いで、水を290L加えてCNFを含有する散布液(CNF濃度0.05%)とした。散布液の一部の様子を図6に示す。図6から、CNFの分散性に優れた散布液を調製することができたことがわかる。
次いで、動力噴霧器を作動させ、貯蔵タンクと循環配管を用いて散布液を循環させながら、噴霧ノズルを用いて、調製した散布液を全量散布した。なお、400Lの散布液を散布するに要した時間は、40分であった。図7に散布液を散布した様子を示す。
散布後の噴霧ノズル及び部材を確認したところ、噴霧ノズルには、CNFが付着していなかった。また、貯蔵タンクの底面に砂等の重量異物が残存していることが確認できた。この結果から、散布装置内の配管や噴霧ノズル等がつまることなく、また、吸入口から重量異物を吸い上げることなく、400Lの散布液を散布することができたといえる。
また、養鶏場の従事者の評価は、餌にかかっても鶏の餌食いが落ちないため助かっている。というものであった。
(Example 1)
Using a device having the same basic configuration as the spraying device for spraying liquid containing fine fibers shown in Figure 1 and members having the same basic configuration as the members shown in Figure 2, a spray liquid is created through the following steps, and this is used for poultry farming. It was dispersed in the field.
First, 10 L of CNF dispersion (CNF concentration 2%, manufactured by Chuetsu Pulp Industries Co., Ltd., trade name: nanoforest-S Farm) and 100 L of water were added to a storage tank to prepare a first dilution. Next, 290 L of water was added to prepare a spray liquid containing CNF (CNF concentration 0.05%). Figure 6 shows a portion of the spray liquid. It can be seen from FIG. 6 that a spray liquid with excellent CNF dispersibility could be prepared.
Next, the power sprayer was operated, and while the spraying liquid was being circulated using the storage tank and circulation piping, the entire amount of the prepared spraying liquid was sprayed using the spray nozzle. The time required to spray 400 L of the spray liquid was 40 minutes. Figure 7 shows how the spray liquid was sprayed.
When the spray nozzle and members were checked after spraying, no CNF was found to have adhered to the spray nozzle. It was also confirmed that heavy foreign matter such as sand remained on the bottom of the storage tank. From this result, it can be said that 400 L of spray liquid could be sprayed without clogging the pipes or spray nozzles in the spraying device, and without drawing up heavy foreign matter from the suction port.
In addition, the chicken farm workers' evaluation is positive because the chickens do not stop eating the feed even if they get caught in the feed. That's what it was.

(比較例1)
図1に示す微細状繊維を含む散布液の散布装置の貯蔵タンクに、CNF分散体(CNF濃度2%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)10Lと水を390L加えて散布液とした。散布液の一部の様子を図8に示す。図8から、CNF同士の凝集体がほぐれず、CNFが沈降したままとなって、散布液とすることができなかった。
(Comparative example 1)
Add 10 L of CNF dispersion (CNF concentration 2%, manufactured by Chuetsu Pulp Industries Co., Ltd., trade name: nanoforest-S Farm) and 390 L of water to the storage tank of the spraying device for the spray liquid containing fine fibers shown in Figure 1. It was made into a spray liquid. Figure 8 shows a portion of the spray liquid. From FIG. 8, the aggregates of CNF were not loosened, and the CNF remained sedimented, and could not be used as a spray liquid.

(実施例2)
実施例1において、400Lの散布液を散布した後に、続けて、同様の操作を6回行い合計約2800Lの散布液を散布した。なお、散布に要した時間は、300分であった。実施例1と同様に、散布後の噴霧ノズル及び部材を確認したところ、噴霧ノズル等には、CNFが付着していなかった。また、貯蔵タンクの底面に砂等の重量異物が残存していることが確認できた。この結果から、噴霧ノズルがつまることなく、また、吸入口から重量異物を吸い上げることなく、約2800Lの散布液を散布することができたといえる。
(Example 2)
In Example 1, after spraying 400 L of the spray liquid, the same operation was performed six times to spray a total of about 2800 L of the spray liquid. The time required for the spraying was 300 minutes. As in Example 1, when the spray nozzle and members were checked after spraying, no CNF was found to have adhered to the spray nozzle or the like. It was also confirmed that heavy foreign matter such as sand remained on the bottom of the storage tank. From this result, it can be said that approximately 2800 L of spray liquid could be sprayed without clogging the spray nozzle or sucking up heavy foreign matter from the suction port.

(実施例3)
CNF分散体(CNF濃度1.57wt%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)を水で希釈し0.1wt%とし、動力噴霧器(株式会社工進社製 型番:ES-10P)に噴霧ノズル(株式会社麻場社製 スーパージェットI型)を接続し噴霧実験を行った。噴霧器の条件は中圧設定、約5L、タンクへの戻し循環を行った。
噴霧ノズルの詳細については以下の通りである。
ノズルヘッド部と0.5mのパイプ部、更にグリップを備えたノズルで、パイプ内部に真鍮製の中子が備わっており、グリップを回すことで中子がノズルヘッド内で前後し、ケーシングと中子の位置が変わり、遠近の調整、更に噴霧の停止が可能なノズルである。中子の先端部の外周部に2本のらせん状の溝が備えてあり、流体はこの溝を通り噴口へ供給されることで常に回転運動しながら噴口2mmφより噴出される。供給圧力1.5MPaで広角時6.0L/min狭角時7.5L/min吐出できるノズルである。
所定量噴霧後、ノズルを取り外して内部状態を確認し、付着したCNFを収集し、105℃で12時間以上乾燥させて付着物重量を測定した。また、噴霧実験前後の残液重量から噴霧量を測定し、噴霧量に対する付着物重量を求めた。また、実施例3~5、比較例2,3について同様に行った。結果を表1に示す。
(Example 3)
A CNF dispersion (CNF concentration 1.57 wt%, manufactured by Chuetsu Pulp Industries Co., Ltd., product name: nanoforest-S Farm) was diluted with water to 0.1 wt%, and a power sprayer (manufactured by Koshinsha Co., Ltd., model number: ES-10P) was used. ) was connected to a spray nozzle (Super Jet I type, manufactured by Asaba Co., Ltd.) and a spray experiment was conducted. The conditions of the sprayer were medium pressure setting, approximately 5 L, and circulation was performed back to the tank.
Details of the spray nozzle are as follows.
This nozzle is equipped with a nozzle head, a 0.5m pipe, and a grip.The inside of the pipe has a brass core, and by turning the grip, the core moves back and forth within the nozzle head, separating the casing and core. It is a nozzle whose position can be changed, distance can be adjusted, and the spray can be stopped. Two spiral grooves are provided on the outer periphery of the tip of the core, and the fluid is supplied to the nozzle through these grooves and is ejected from the 2 mm diameter nozzle while constantly rotating. This nozzle can discharge 6.0L/min at wide angle and 7.5L/min at narrow angle at a supply pressure of 1.5MPa.
After spraying a predetermined amount, the nozzle was removed to check the internal condition, and the adhered CNF was collected, dried at 105°C for 12 hours or more, and the weight of the adhered substance was measured. In addition, the amount of spray was measured from the weight of the remaining liquid before and after the spray experiment, and the weight of deposits relative to the amount of spray was determined. Further, the same procedure was carried out for Examples 3 to 5 and Comparative Examples 2 and 3. The results are shown in Table 1.

(実施例4)
CNF分散体(CNF濃度1.57wt%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)を水で希釈し0.1%wt%とし、動力噴霧器(株式会社工進社製 型番:ES-10P)に噴霧ノズル(株式会社工進社製 泡状除草用PA-284)を接続し噴霧実験を行った。噴霧器の条件は中圧設定、約5L、タンクへの戻し循環を行った。
噴霧ノズルの詳細については以下の通りである。
1つのノズルヘッドを備えたノズルで、流体は8mmφの開口部を通り、更に1mmφの開口部を経てノズルヘッドへ供給され、ノズルヘッド側面に外気取り込み用の1mmφの開口を2カ所備え、1mmφからの供給圧力で外気を取り込みながら泡状になり、5.3mmφの開口を通過して噴射口へ供給される。2mm角の噴口入口には、更に2.7mmφの開口部が2個備わり、ここを通過後に最終的に噴霧されるノズルである。
(Example 4)
A CNF dispersion (CNF concentration 1.57 wt%, manufactured by Chuetsu Pulp Industries Co., Ltd., product name: nanoforest-S Farm) was diluted with water to 0.1% wt%, and then mixed with a power sprayer (manufactured by Koshinsha Co., Ltd., model number: ES). -10P) was connected to a spray nozzle (PA-284 for foam weed control manufactured by Koshinsha Co., Ltd.) and a spraying experiment was conducted. The conditions of the sprayer were medium pressure setting, approximately 5 L, and circulation was performed back to the tank.
Details of the spray nozzle are as follows.
This is a nozzle with one nozzle head, and the fluid passes through an 8mmφ opening and then is supplied to the nozzle head through a 1mmφ opening.There are two 1mmφ openings on the side of the nozzle head for taking in outside air, and from 1mmφ It becomes a bubble while taking in outside air under the supply pressure of , and is supplied to the injection port through a 5.3mmφ opening. The 2mm square nozzle inlet is further equipped with two 2.7mmφ openings, which are the final nozzles that spray after passing through these openings.

(実施例5)
CNF分散体(CNF濃度1.57wt%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)を水で希釈し0.1wt%とし、動力噴霧器(株式会社工進社製 型番:ES-10P)に噴霧ノズル(株式会社丸山製作所社製 BigM)を接続し噴霧実験を行った。噴霧器の条件は中圧設定、約5L、タンクへの戻し循環を行った。
噴霧ノズルの詳細については以下の通りである。
ノズルヘッド内部に旋回する中子を備えたノズルで、旋回部の外形に沿って、2本の螺旋状の溝が備えてあり、流体はこの溝を通り0.9mmφの噴口へ供給されることで中子が回転するノズルである。供給圧力1.5MPaで0.72L/min吐出できるノズルであり、噴口に対する流量が少ない。
(Example 5)
A CNF dispersion (CNF concentration 1.57 wt%, manufactured by Chuetsu Pulp Industries Co., Ltd., product name: nanoforest-S Farm) was diluted with water to 0.1 wt%, and a power sprayer (manufactured by Koshinsha Co., Ltd., model number: ES-10P) was used. ) was connected to a spray nozzle (BigM, manufactured by Maruyama Seisakusho Co., Ltd.) and a spraying experiment was conducted. The conditions of the sprayer were medium pressure setting, approximately 5 L, and circulation was performed back to the tank.
Details of the spray nozzle are as follows.
This nozzle is equipped with a core that rotates inside the nozzle head.There are two spiral grooves along the outer shape of the rotating part, and the fluid passes through these grooves and is supplied to the 0.9mmφ nozzle. This is a nozzle with a rotating core. This nozzle can discharge 0.72L/min at a supply pressure of 1.5MPa, and the flow rate to the nozzle is small.

(比較例2)
CNF分散体(CNF濃度1.57wt%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)を水で希釈し0.1wt%とし、動力噴霧器(株式会社工進社製 型番:ES-10P)に噴霧ノズル(株式会社工進社製 縦型二頭口PA-292)を接続し噴霧実験を行った。噴霧器の条件は中圧設定、約5L、タンクへの戻し循環を行った。
噴霧ノズルの詳細については以下の通りである。
2つのノズルヘッドを備えたノズルで、内部に2層こし網を備え、流体は8mmの開口部を通り、内部に2層こし網へ供給され、第一網(丸孔D:0.5mmφ,P:1.2mm,開口率27%の45°千鳥パンチングプレート)、第2網(1辺4.5mmの正方形の頂点に4個の1.6mmφの穴を備える)を通り、噴口1.1mmより噴霧されるノズルである。
(Comparative example 2)
A CNF dispersion (CNF concentration 1.57 wt%, manufactured by Chuetsu Pulp Industries Co., Ltd., product name: nanoforest-S Farm) was diluted with water to 0.1 wt%, and a power sprayer (manufactured by Koshinsha Co., Ltd., model number: ES-10P) was used. ) was connected to a spray nozzle (vertical double-head PA-292 manufactured by Koshinsha Co., Ltd.) and a spray experiment was conducted. The conditions of the sprayer were medium pressure setting, approximately 5 L, and circulation was performed back to the tank.
Details of the spray nozzle are as follows.
A nozzle with two nozzle heads, equipped with a two-layer strainer inside, the fluid passes through an 8mm opening, is supplied to the two-layer strainer inside, and the first screen (round hole D: 0.5mmφ, P :1.2mm, 45° staggered punching plate with an aperture ratio of 27%), a nozzle that passes through the second mesh (four 1.6mmφ holes at the apex of a 4.5mm square on a side) and sprays from a 1.1mm nozzle. It is.

(比較例3)
CNF分散体(CNF濃度1.57wt%、中越パルプ工業株式会社製、商品名:nanoforest-Sファーム)を水で希釈し0.1%wt%とし、動力噴霧器(株式会社工進社製 型番:ES-10P)に噴霧ノズル(ヤマホ工業株式会社製 スーパーズームP-700)を接続し噴霧実験を行った。噴霧器の条件は中圧設定、約5L、タンクへの戻し循環を行った。
噴霧ノズルの詳細については以下の通りである。
ノズルヘッド部と1m以上のパイプ部、更にグリップを備えたノズルである。グリップを回すことでノズルヘッド手前の吹き出し口が前後に出入りすることでノズルとの間隔が短長し、噴口からのスプレー角度を調節できる。ケーシング内で前後し、ケーシングと中子の位置が変わり、遠近の調整、更に噴霧の停止が可能なノズルである。中子の先端部の外周部に2本の直線状の溝が備えてあり、流体はこの溝を通り噴口へ供給されることで常に回転運動しながら噴口2mmφより噴出される。中子の側面には2カ所の凸部が配置されている。供給圧力1.5MPaで広角時5.76L/min狭角時7.17L/min吐出できるノズルである。
(Comparative example 3)
A CNF dispersion (CNF concentration 1.57 wt%, manufactured by Chuetsu Pulp Industries Co., Ltd., product name: nanoforest-S Farm) was diluted with water to 0.1% wt%, and then mixed with a power sprayer (manufactured by Koshinsha Co., Ltd., model number: ES). -10P) was connected to a spray nozzle (Superzoom P-700 manufactured by Yamaho Industries, Ltd.) and a spraying experiment was conducted. The conditions of the sprayer were medium pressure setting, approximately 5 L, and circulation was performed back to the tank.
Details of the spray nozzle are as follows.
It is a nozzle equipped with a nozzle head part, a pipe part of 1 m or more, and a grip. By turning the grip, the outlet in front of the nozzle head moves back and forth, allowing you to shorten or lengthen the distance between the nozzle and the spray angle from the nozzle. This nozzle moves back and forth within the casing, changing the position of the casing and core, making it possible to adjust distance and stop spraying. There are two linear grooves on the outer periphery of the tip of the core, and the fluid is supplied to the nozzle through these grooves and is ejected from the 2 mm diameter nozzle while constantly rotating. Two protrusions are placed on the side of the core. This nozzle can discharge 5.76L/min at wide angle and 7.17L/min at narrow angle with a supply pressure of 1.5MPa.

Figure 0007399208000001
Figure 0007399208000001

ノズル内部に漉し網が付いた比較例2は内部付着が多い結果となった。時間当り噴霧量が少ないと管内流速が落ち付着しやすい傾向であるが実施例5では付着量が抑えられた。ノズルまでの導入配管が長く、沈降しやすい持ち手つきの実施例3と比較例3では、実施例3の方が良好だった。実施例3,5の結果より、回転機構を有する噴霧ノズルでは良好な噴霧状態を維持できる。また流量の少ないと詰まり易い傾向となるが、実施例4では巻き込むエアによりCNFの凝集が抑えられている。
以上より、外気取り込み口を備える泡状ノズル、螺旋状の溝を有する中子を備えた回転機構を有する噴霧ノズルが適切であることが明らかとなった。また、旋回誘導部の溝は螺旋状が良く、溝幅は広い方が良いことが明らかとなった。
Comparative Example 2, which had a strainer screen inside the nozzle, resulted in a lot of internal adhesion. When the amount of spray per hour is small, the flow velocity in the pipe decreases and there is a tendency for adhesion to occur, but in Example 5, the amount of adhesion was suppressed. Between Example 3 and Comparative Example 3, which had a long introduction pipe to the nozzle and a handle that easily settled, Example 3 was better. From the results of Examples 3 and 5, the spray nozzle having a rotation mechanism can maintain a good spray state. Furthermore, if the flow rate is low, clogging tends to occur, but in Example 4, the agglomeration of CNF is suppressed by the air involved.
From the above, it has become clear that a foam nozzle with an outside air intake port and a spray nozzle with a rotating mechanism including a core with a spiral groove are suitable. It has also been found that the spiral shape of the groove in the turning guiding portion is better, and the wider the groove width is, the better.

Claims (5)

微細状繊維を含む散布液を散布する散布装置であって、
少なくとも、散布液投入口と循環戻り口とを備える貯蔵タンクと、
噴霧ノズルと、
循環口と、吐出口と、吸水口とを備える動力噴霧器と、
前記循環口に一端が接続し、他端を前記循環戻り口に接続する循環配管と、
前記吐出口に一端が接続し、他端が前記噴霧ノズルに接続した吐出配管と、
前記吸水口に一端が接続し、他端が前記貯蔵タンクに接続した吸水配管と、
前記貯蔵タンクに接続した吸水配管の吸込口に、前記貯蔵タンクの底面と前記吸込口との距離を維持するための部材とを備え、
前記噴霧ノズルは、螺旋状の溝を有する中子を備えた回転機構を有する噴霧ノズル又は、外気取り込み口を備えた泡状ノズルであり、
前記循環戻り口を介して、前記動力噴霧器と循環配管を用いて貯蔵タンク中の微細状繊維を含む散布液を循環させる微細状繊維を含む散布液の散布装置。
A spraying device that sprays a spray liquid containing fine fibers,
a storage tank comprising at least a spray liquid input port and a circulation return port;
a spray nozzle;
A power sprayer including a circulation port, a discharge port, and a water intake port;
circulation piping having one end connected to the circulation port and the other end connected to the circulation return port;
a discharge pipe having one end connected to the discharge port and the other end connected to the spray nozzle;
a water intake pipe whose one end is connected to the water intake port and whose other end is connected to the storage tank;
A member for maintaining a distance between the bottom surface of the storage tank and the suction port is provided at the suction port of the water suction pipe connected to the storage tank,
The spray nozzle is a spray nozzle having a rotation mechanism equipped with a core having a spiral groove, or a foam nozzle equipped with an outside air intake port,
A spraying device for a spray liquid containing fine fibers that circulates the spray liquid containing fine fibers in a storage tank using the power sprayer and circulation piping through the circulation return port.
微細状繊維を含む散布液を散布する散布装置であって、
少なくとも、散布液投入口を備える貯蔵タンクと、
噴霧ノズルと、
循環口と、吐出口と、吸水口とを備える動力噴霧器と、
前記循環口に一端が接続し、他端を前記散布液投入口に接続する循環配管と、
前記吐出口に一端が接続し、他端が前記噴霧ノズルに接続した吐出配管と、
前記吸水口に一端が接続し、他端が前記貯蔵タンクに接続した吸水配管と、
前記貯蔵タンクに接続した吸水配管の吸込口に、前記貯蔵タンクの底面と前記吸込口との距離を維持するための部材とを備え、
前記噴霧ノズルは、螺旋状の溝を有する中子を備えた回転機構を有する噴霧ノズル又は、外気取り込み口を備えた泡状ノズルであり、
前記散布液投入口を介して、前記動力噴霧器と循環配管を用いて貯蔵タンク中の微細状繊維を含む散布液を循環させる微細状繊維を含む散布液の散布装置。
A spraying device that sprays a spray liquid containing fine fibers,
at least a storage tank comprising a spray liquid inlet;
a spray nozzle;
A power sprayer including a circulation port, a discharge port, and a water intake port;
a circulation pipe whose one end is connected to the circulation port and whose other end is connected to the spray liquid input port;
a discharge pipe having one end connected to the discharge port and the other end connected to the spray nozzle;
a water intake pipe whose one end is connected to the water intake port and whose other end is connected to the storage tank;
A member for maintaining a distance between the bottom surface of the storage tank and the suction port is provided at the suction port of the water suction pipe connected to the storage tank,
The spray nozzle is a spray nozzle having a rotation mechanism equipped with a core having a spiral groove, or a foam nozzle equipped with an outside air intake port,
A spraying device for a spraying liquid containing fine fibers, which circulates the spraying liquid containing fine fibers in a storage tank using the power sprayer and circulation piping through the spraying liquid input port.
微細状繊維を含有する分散体を、前記分散体の容量の5~10倍の水を用いて希釈して、第一の希釈体を調製する第一の希釈工程と、
第一の希釈体を水で希釈して所定の濃度の微細状繊維を含有する散布液とする第二の希釈工程とを有する混合工程と、
前記微細状繊維を含有する散布液を、貯蔵タンクと、循環配管と、動力噴霧器とを利用して、循環させる循環工程と、
噴霧ノズルを利用して、所定の場所へ散布する散布工程と
を備える微細状繊維を含む散布液の散布装置を用いた散布方法。
A first dilution step of preparing a first dilution by diluting a dispersion containing fine fibers with water in an amount of 5 to 10 times the volume of the dispersion;
a second dilution step of diluting the first diluent with water to obtain a spray liquid containing fine fibers at a predetermined concentration;
a circulation step of circulating the spray liquid containing the fine fibers using a storage tank, circulation piping, and a power sprayer;
A spraying method using a spraying device for spraying a spray liquid containing fine fibers, which comprises a spraying step of spraying to a predetermined location using a spray nozzle.
微細状繊維の濃度が0.1~15%の範囲にある微細状繊維を含有する分散体を水で希釈して第一の希釈体を調製する第一の希釈工程と、
第一の希釈体を、第一の希釈体の等倍以上の水で希釈して、微細状繊維の濃度が0.001~0.5%の濃度の微細状繊維を含有する散布液とする第二の希釈工程とを有する混合工程と、
前記微細状繊維を含有する散布液を、貯蔵タンクと、循環配管と、動力噴霧器とを利用して、循環させる循環工程と、
噴霧ノズルを利用して、所定の場所へ散布する散布工程と
を備える微細状繊維を含む散布液の散布装置を用いた散布方法。
a first dilution step of preparing a first diluted body by diluting a dispersion containing fine fibers with a concentration of fine fibers in the range of 0.1 to 15% with water;
The first diluent is diluted with water in an amount equal to or more than the first diluent to obtain a spray liquid containing fine fibers with a fine fiber concentration of 0.001 to 0.5%. a mixing step having a second dilution step;
a circulation step of circulating the spray liquid containing the fine fibers using a storage tank, circulation piping, and a power sprayer;
A spraying method using a spraying device for spraying a spray liquid containing fine fibers, which comprises a spraying step of spraying to a predetermined location using a spray nozzle.
前記循環工程は、常時循環させて、微細状繊維を含む散布液が常に流動状態である、請求項3又は4に記載の微細状繊維を含む散布液の散布装置を用いた散布方法。 5. The spreading method using the spraying device for a spraying liquid containing fine fibers according to claim 3 or 4, wherein the circulation step is performed by constantly circulating the spraying liquid containing fine fibers so that the spray liquid containing fine fibers is always in a fluid state.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002143662A (en) 2000-11-13 2002-05-21 Tokushu Paper Mfg Co Ltd Method and apparatus for storing and/or dispersing slurry
JP2017006857A (en) 2015-06-22 2017-01-12 花王株式会社 Method and device for producing slurry composition
JP2020138346A (en) 2019-02-27 2020-09-03 理想科学工業株式会社 Stirrer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002143662A (en) 2000-11-13 2002-05-21 Tokushu Paper Mfg Co Ltd Method and apparatus for storing and/or dispersing slurry
JP2017006857A (en) 2015-06-22 2017-01-12 花王株式会社 Method and device for producing slurry composition
JP2020138346A (en) 2019-02-27 2020-09-03 理想科学工業株式会社 Stirrer

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