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JP2003010663A - Material atomizing device - Google Patents

Material atomizing device

Info

Publication number
JP2003010663A
JP2003010663A JP2001203318A JP2001203318A JP2003010663A JP 2003010663 A JP2003010663 A JP 2003010663A JP 2001203318 A JP2001203318 A JP 2001203318A JP 2001203318 A JP2001203318 A JP 2001203318A JP 2003010663 A JP2003010663 A JP 2003010663A
Authority
JP
Japan
Prior art keywords
holes
raw material
main body
disk
groove
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001203318A
Other languages
Japanese (ja)
Other versions
JP3696808B2 (en
Inventor
Yoshinobu Hattori
吉延 服部
Yukinobu Takahashi
幸悦 高橋
Yasushi Omura
康 大村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SG ENGINEERING KK
YOSHIDA KIKAI CO Ltd
Original Assignee
SG ENGINEERING KK
YOSHIDA KIKAI CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SG ENGINEERING KK, YOSHIDA KIKAI CO Ltd filed Critical SG ENGINEERING KK
Priority to JP2001203318A priority Critical patent/JP3696808B2/en
Publication of JP2003010663A publication Critical patent/JP2003010663A/en
Application granted granted Critical
Publication of JP3696808B2 publication Critical patent/JP3696808B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To precisely cope with various demands on various materials, such as the particle size distribution and increase in throughput, when materials are atomized. SOLUTION: A pair of discs A, B are laid so that their P sides are superposed, and are incorporated in a cylinder body of a device body that atomizes a pressurized material. A small number of, for example two, through holes are formed in the discs A, B so that the holes are positioned not to be superposed, and these through holes are communicated through a groove formed on at least one of the P sides of the discs A, B.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、食品、化学、医薬
等の各業界で扱う物質を微粒化する装置に関し、特に、
物質を、乳化、分散又は破砕の状態にて、ミクロン台又
はそれ以下の均一(又は均質)的な粒子径に微粒化し
て、安定した粒度分布のものを得る装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for atomizing substances handled in the food, chemical, pharmaceutical and other industries, and more particularly,
The present invention relates to an apparatus for atomizing a substance in a state of emulsification, dispersion or crushing into a uniform (or homogeneous) particle size on the order of microns or less to obtain a stable particle size distribution.

【0002】[0002]

【従来の技術】従来の物質の微粒化装置として、最近に
おいて公開された特開2001−29776号公報のも
のがある。これは、原料供給口に供給された原料を加圧
して装置本体に送り、この本体で前記原料中の物質を微
粒化して取出す物質の微粒化装置において、前記本体
は、入口及び出口付きの円筒体と、この円筒体に面一に
重ね合わされて組込まれる少なくとも2個の円板とを有
し、前記各円板には同一又は類似の態様で整列した多数
の貫通孔と、前記面上で各貫通孔を接続する多数の溝と
が設けられ、前記講は、前記各円板が重ね合わされた状
態で多数の個所で一方の円板の溝が他方の円板の溝に対
して前記面上で互いに交差するようになっていることを
特徴とするものである。
2. Description of the Related Art As a conventional atomizing device for substances, there is a device disclosed in Japanese Patent Laid-Open No. 2001-29776, which was recently published. This is a material atomization device that pressurizes the raw material supplied to the raw material supply port and sends it to the main body of the device, and atomizes the substance in the raw material by this main body, in which the main body is a cylinder with an inlet and an outlet. A body and at least two discs which are mounted on the cylinder so as to be flush with each other, and each disc has a large number of through holes aligned in the same or similar manner, and on the face. A large number of grooves for connecting the respective through holes are provided, and in the above-mentioned lecture, the grooves of one disk are arranged at a large number of positions in a state where the respective disks are overlapped with each other and the surfaces of the grooves are the same as the grooves of the other disk. It is characterized by intersecting with each other above.

【0003】この従来のものは、前記構成により処理加
圧力をそれほど大きくしなくても所望量の微粒化処理を
可能とするという利点があるものである。
This conventional device has an advantage in that it is possible to perform a desired amount of atomization processing without increasing the processing pressure so much due to the above structure.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前記従
来のものは、前述の利点を有するが、装置本体を小型に
する場合、各円板共、多数の貫通孔を有するが故に製作
加工が難かしいという欠点がある。一方、貫通孔及び溝
を極力少なくすれば加工容易となるが、その場合には、
物質を扱う各業界の微粒化に対する粒径要望などに沿え
ず、融通性、設計の自由度において満足できないものと
なる欠点がある。
However, although the above-mentioned conventional device has the above-mentioned advantages, when the device main body is downsized, since each disk has a large number of through holes, the manufacturing process is difficult. There is a drawback that. On the other hand, if the number of through holes and grooves is reduced as much as possible, processing becomes easier.
There is a drawback that the flexibility and the degree of freedom in design cannot be satisfied because the industry does not meet the particle size requirements for atomization in each industry that handles substances.

【0005】本発明は、装置を小型にできると共に、製
作加工も容易で、かつ、各種物質の処理粒径や処理量増
大といった多様な要求に対して的確に対処でき、汎用
性、融通性、設計の自由度においても満足できる物質の
微粒化装置を提供することを目的とするものである。
According to the present invention, the apparatus can be downsized, the manufacturing process can be easily performed, and various requirements such as an increase in the treatment particle size and the treatment amount of various substances can be appropriately dealt with, and the versatility, versatility, and It is an object of the present invention to provide an atomizer for a substance which is satisfactory in terms of design freedom.

【0006】[0006]

【課題を解決するための手段】本発明は前記目的を達成
するために、請求項1は原料供給口に供給される原料を
加圧して本体に送り、この本体で前記原料中の物質を微
粒化して取出す物質の微粒化装置において、前記本体
は、入口及び出口付きの円筒体と、この円筒体に位置合
わせされ面一にP面にて重ねられ組込まれる一対の円板
A,Bを有し、該円板A,Bには互いに反対側の半円部
に2個の貫通孔が夫々設けられ、また、該円板A,Bの
いずれか一方のP面には当該一方の2個の貫通孔と接続
し、かつ、横直径線XX及び縦直径線YYに対し対称な
所定の形状の溝が設けられており、円板A,BをP面で
重ねたとき、前記溝の両端部が他方の2個の貫通孔に連
通するようになっていることを特徴とし、請求項2は原
料供給口に供給される原料を加圧して本体に送り、この
本体で前記原料中の物質を微粒化して取出す物質の微粒
化装置において、前記本体は、入口及び出口付きの円筒
体と、この円筒体に位置合わせされ面一にP面にて重ね
られ組込まれる一対の円板A,Bを有し、該円板A,B
は横直径線XX及び縦直径線YYに対して対称にかつ互
いに重ならない位置に2〜6個の貫通孔を有してこれら
の貫通孔がP面において夫々の円板のP面に設けられた
直線状の溝により接続しており、円板A,BをP面で重
ねたとき前記両方の溝が1〜5個の交差点Kで交差する
ことにより互いに連通するようになっていることを特徴
とするものである。
In order to achieve the above-mentioned object, the present invention relates to claim 1 in which a raw material supplied to a raw material supply port is pressurized and sent to a main body, and the main body finely granulates the substance in the raw material. In the atomizer of the substance to be atomized and taken out, the main body has a cylindrical body with an inlet and an outlet, and a pair of discs A and B which are aligned with the cylindrical body and are superposed on the P plane and flush with each other. However, the disks A and B are respectively provided with two through holes in semicircular portions on the opposite sides, and the P surface of either one of the disks A and B has two through holes. Is provided with a groove having a predetermined shape which is connected to the through hole and is symmetrical with respect to the horizontal diameter line XX and the vertical diameter line YY. When the disks A and B are stacked on the P plane, both ends of the groove are formed. The portion is adapted to communicate with the other two through holes, and the second aspect is to supply the raw material supply port. In the atomizer of the substance, which pressurizes the raw material and sends it to the main body, and atomizes the substance in the raw material by this main body, the main body is a cylindrical body with an inlet and an outlet, and a surface aligned with the cylindrical body. A pair of discs A and B which are superposed and assembled on the P plane
Has 2 to 6 through holes which are symmetrical with respect to the horizontal diameter line XX and the vertical diameter line YY and do not overlap each other, and these through holes are provided in the P plane of each disc in the P plane. Are connected by a linear groove, and when the disks A and B are overlapped with each other on the P plane, both of the grooves intersect each other at 1 to 5 intersections K so that they communicate with each other. It is a feature.

【0007】[0007]

【作用】請求項1では、円板Aの上半円にある2個の貫
通孔に流入した原料(流体)が円板BのP面と突き当っ
た後に直角に向きを変え円板Aの、例えば、8の字状の
溝を通り、その溝の両端部で円板Bの下半円にある2個
の貫通孔と連通し、ここで、また直角に向きを変え、こ
の貫通孔から流れ去る。これらの流れにおいて、加圧流
体中の物質は、貫通孔、溝等での合流衝突、分流拡張に
より所望の粒径(粒度分布により定まる)のものに微粒
化される。円板の材料が超硬質セラミックス、焼結人工
ダイヤモンド又は単結晶ダイヤモンドであって、その大
きさが直径40mmφ、厚さ5mmの硬い小さな円板のもの
においても容易に1〜2mmφの孔径の穿孔、0.5mm
幅、0.2mm深さの溝の加工ができる。そして孔径や溝
の形状を変えることで、粒径及び流量(処理量)増大の
要望に応えることができる。
According to the first aspect of the invention, the raw material (fluid) flowing into the two through holes in the upper half circle of the disk A collides with the P surface of the disk B and then changes its direction at a right angle. , For example, through a figure-eight groove and communicate with two through-holes in the lower half circle of the disk B at both ends of the groove, and turn here again at right angles, and from this through-hole Flow away. In these flows, the substance in the pressurized fluid is atomized into particles having a desired particle size (determined by the particle size distribution) by merging collisions in through holes, grooves, etc. and diversion expansion. Even if the material of the disc is ultra-hard ceramic, sintered artificial diamond or single crystal diamond, and the size of the hard disc is 40 mmφ in diameter and 5 mm in thickness, it is easy to perforate holes with a diameter of 1-2 mmφ. 0.5 mm
A groove with a width of 0.2 mm can be processed. By changing the hole diameter and the shape of the groove, it is possible to meet the demand for increasing the particle diameter and the flow rate (processing amount).

【0008】請求項2では、例えば、円板Aの4個の貫
通孔に等分に入った原料流れは、円板BのP面に突き当
って直角に向きを変え、円板AのH形状の溝に入りこ
み、その中心で互いに衝突した後に、交差点K(この場
合は1個)で、今度は円板BのI形状の溝に入り、両方
に直角に分れ、円板Bの2個の貫通孔から、再び直角に
向きを変えて流出する。この場合は、貫通孔の数が多い
だけ、融通性に富み、その分、加工も難かしくなるが、
貫通孔の位置及び数を規定してあるので、加工の困難性
を和らげることができる。そして、貫通孔の孔径、数は
勿論、溝の寸法や形状を変えることで、やはり、粒径要
望等に応えることができる。
In the second aspect, for example, the raw material flow equally distributed into the four through holes of the disk A hits the P surface of the disk B and changes its direction at a right angle, so that the H of the disk A is changed. After entering the groove of the shape and colliding with each other at the center, at the intersection K (one in this case), this time into the groove of the shape of disk B, split at right angles to both, From each of the through holes, it turns again at a right angle and flows out. In this case, as the number of through holes is large, it is rich in flexibility, and accordingly, processing becomes difficult,
Since the position and the number of the through holes are defined, it is possible to reduce the difficulty of processing. By changing not only the hole diameter and number of the through holes but also the size and shape of the grooves, it is possible to meet the demands for the particle diameter.

【0009】[0009]

【発明の実施の形態】図1のシステム図に於て、1は原
料(物質と液体の混合物)の供給口、2は原料を加圧す
る高圧ポンプ、3は本体、4は原料中の物質が微粒化さ
れたもの、即ち、微粒化製品の受入器である。
BEST MODE FOR CARRYING OUT THE INVENTION In the system diagram of FIG. 1, 1 is a feed port for a raw material (mixture of substance and liquid), 2 is a high-pressure pump for pressurizing the raw material, 3 is a main body, and 4 is a substance in the raw material. An atomized product, that is, a receiver for atomized products.

【0010】図2は、図1における本体3の断面図であ
り、本体3は入口側の円筒6と出口側の円筒7をボルト
8で締結してなる1個の円筒体5内に、位置決め用のピ
ン9で位置合わせされ、P面で面一に重ねられ組込まれ
た一対の円板A10と円板B11とを有する。円板A,
Bは共に直径40mmφ、厚さ5mm、の超硬質セラミック
ス製である。
FIG. 2 is a cross-sectional view of the main body 3 in FIG. 1, and the main body 3 is positioned in one cylindrical body 5 formed by fastening a cylinder 6 on the inlet side and a cylinder 7 on the outlet side with bolts 8. It has a pair of discs A10 and B11 which are aligned by a pin 9 for use and are mounted so as to be flush with each other on the P-plane. Disk A,
Both B are made of ultra-hard ceramics with a diameter of 40 mm and a thickness of 5 mm.

【0011】本発明において、一対の円板A,Bは特許
請求の範囲に記載してある請求項1と請求項2とに対応
するように、実施の形態が第1形態と第2形態とに分か
れる。
In the present invention, the pair of discs A and B correspond to claims 1 and 2 described in the claims, and the embodiment has a first form and a second form. Divided into

【0012】〔第1形態〕図3〜図7は第1形態におけ
る第1の実施例のものを示す。図3は円板A10と円板
B11がP面で合わされる前の状態を模式的に示す斜視
図である。図3において、円板A10には横直径線XX
より上の上半円部に2個の貫通孔(約1.5mmφ)12
が縦直径線YYに対して対称に設けられ、その合わせ面
であるP面には、これらの貫通孔12と接続し(交わ
り)、かつ、横直径線XX及び縦直径線YYに対して対
称となるように、上下一の字線を2個の円形で接続した
大略8の字状の溝(幅1mm、深さ0.5mm)13が設け
られている(円板AのP面を示す図4参照方)。また、
円板B11には、P面に何等溝を有せず、円形A10の
貫通孔12と対称の位置、即ち、横直径線XXより下の
下半円部に、2個の貫通孔(円板Aのものより若干大径
の約2mmφ)14が設けられている。円板BのP面を示
す図6参照方)。この貫通孔14は、円板A10と合わ
せたときその溝13の両末端部13Aに連通するように
なっている。なお、図3、4及び6において、15はピ
ン9にはめこまれて位置決めとなる穴である。
[First Embodiment] FIGS. 3 to 7 show the first embodiment of the first embodiment. FIG. 3 is a perspective view schematically showing a state before the disc A10 and the disc B11 are brought together on the P surface. In FIG. 3, the disk A10 has a lateral diameter line XX.
Two through-holes (about 1.5 mmφ) 12 in the upper half circle above
Are provided symmetrically with respect to the vertical diameter line YY, and the P surface, which is the mating surface, is connected (intersects) with these through holes 12 and is symmetrical with respect to the horizontal diameter line XX and the vertical diameter line YY. As shown in the figure, an approximately 8-shaped groove (width 1 mm, depth 0.5 mm) 13 in which upper and lower one-shaped lines are connected in two circles is provided (the P surface of the disk A is shown. (See FIG. 4). Also,
The disk B11 does not have any groove on the P surface, and has two through holes (disks) at a position symmetrical with the through hole 12 of the circle A10, that is, in the lower semicircle below the lateral diameter line XX. A diameter of about 2 mm φ) 14 which is slightly larger than that of A is provided. (Refer to FIG. 6 showing the P surface of the disk B). The through hole 14 communicates with both end portions 13A of the groove 13 when combined with the disc A10. It should be noted that in FIGS. 3, 4 and 6, reference numeral 15 is a hole which is fitted into the pin 9 for positioning.

【0013】第1形態における第1実施例のものの作用
は次のとおりである。即ち、図3において、これらが図
2のように組込まれたものとすると、円板A10の貫通
孔12に入った原料流れ(図3矢印Dで示す)は円板B
11の合わせP面の平面部に当ってP面内の溝13の方
向に直角に曲げられ、かつ、8の字形に流れ、両末端部
13Aで円板B11の貫通孔14に連通しここで再び直
角に曲げられて流出する(矢印Eで示す)。
The operation of the first embodiment of the first mode is as follows. That is, in FIG. 3, assuming that these are assembled as shown in FIG. 2, the raw material flow (shown by the arrow D in FIG. 3) entering the through hole 12 of the disk A10 is the disk B.
11 is bent at a right angle in the direction of the groove 13 in the P-plane by hitting the flat surface of the mating P-plane, and flows in a figure 8 shape, and communicates with the through hole 14 of the disk B11 at both end portions 13A. It is bent again at a right angle and flows out (indicated by arrow E).

【0014】これにより、原料中の物質は、高圧、高速
流での衝突、合流、分流、拡張により所望の粒径に微粒
化される。両円板A,B共に貫通孔の数は少なく、ま
た、円板Bには溝が設けられていない故に加工容易であ
り、極力、小型化できる長所がある。
As a result, the substance in the raw material is atomized to a desired particle size by collision with high pressure and high speed flow, merging, diversion and expansion. Both discs A and B have a small number of through holes, and since disc B is not provided with a groove, it is easy to process and has the advantage that it can be miniaturized as much as possible.

【0015】図8〜10は第1形態における第2実施例
を示す。図8に示すように、円板A10には縦直径線Y
Yの右半円部に2個の貫通孔12があり、これら貫通孔
12と接続し横直径線XX及び縦直径線YYに対し対称
のV字と逆V字を重ねた形状の溝13が設けられてい
る。一方、図10に示すように、円板B11には、縦直
径線YYの右半円部に円板A10と同様位置に但し孔径
は若干大きい2個の貫通孔14があり、両円板A,Bを
位置決め用の穴15を基準に重ね合わせたときには、図
8に鎖線で示すように、貫通孔14のある半円部が左半
円部となり、これにより、溝13の両端部13Aと連通
するものである。
8 to 10 show a second embodiment of the first mode. As shown in FIG. 8, the disc A10 has a vertical diameter line Y.
There are two through holes 12 in the right semicircle of Y, and a groove 13 that is connected to these through holes 12 and has a V-shape and an inverted V-shape that are symmetrical with respect to the horizontal diameter line XX and the vertical diameter line YY is formed. It is provided. On the other hand, as shown in FIG. 10, the disk B11 has two through holes 14 at the same position as the disk A10 in the right semicircle of the vertical diameter line YY, but with a slightly larger hole diameter. , B when the positioning holes 15 are overlapped with each other, the semicircular portion having the through hole 14 becomes the left semicircular portion as shown by the chain line in FIG. It is in communication.

【0016】図11〜14は第1形態における第3実施
例を示す。これらの図より分るように、円板A10及び
円板B11共に位置決め用の穴15が縦直径線YYの上
方に位置し、2個の貫通孔12及び14が共に左半円部
にあるが、重ね合わせたときは互いに反対の半円部に位
置するものであり、また、溝13が図11で示すよう
に、W字及び逆W字を重ねた形状のものであり、やは
り、縦横直径線に対して対称であって、その両端部13
Aで、貫通孔14に連通するものとなっている。
11 to 14 show a third embodiment of the first mode. As can be seen from these figures, the positioning hole 15 is located above the longitudinal diameter line YY for both the disk A10 and the disk B11, and the two through holes 12 and 14 are both located in the left semicircle. , They are located in opposite semi-circular portions when they are overlapped with each other, and the groove 13 has a shape in which W-shaped and inverted W-shaped are stacked as shown in FIG. It is symmetric with respect to the line and its both ends 13
A communicates with the through hole 14.

【0017】このように、第1形態のものは、第1実施
例、第2実施例、そして第3実施例の順に流量増大に対
処できると共に、貫通孔の数が円板A,B共に互いに反
対の半円部に2個設けるだけであるため、小型のもので
の製作加工が容易となるものである。
As described above, in the first embodiment, the flow rate increase can be dealt with in the order of the first embodiment, the second embodiment, and the third embodiment, and the numbers of the through holes of both the disks A and B are mutually different. Since only two are provided in the opposite semi-circular portions, it is easy to manufacture and process with a small size.

【0018】〔第2形態〕図15は本発明による第2形
態のものであって、この第2形態における第1、第2及
び第3の各実施例を一括して示す模式的斜視図である。
この図15において一対の円板A,Bの位置合わせ穴の
図示を省略してあるが、例えば上段(a)ではP面に互
いに面一に組込まれるものを示してある。そして、この
上段の(a)は図16〜19に示す第1実施例、中段の
(b)は図20〜23に示す第2実施例、下段の(c)
は図24〜27に示す第3実施例を表わし、(a)
(b)(c)の順に微粒化流量(処理量)が増大するの
に対処するものとなっている。
[Second Embodiment] FIG. 15 is a schematic perspective view showing a second embodiment according to the present invention and collectively showing the first, second and third embodiments of the second embodiment. is there.
In FIG. 15, the alignment holes of the pair of discs A and B are not shown, but for example, in the upper stage (a), the P-planes are shown flush with each other. Then, the upper part (a) is the first embodiment shown in FIGS. 16 to 19, the middle part (b) is the second embodiment shown in FIGS. 20 to 23, and the lower part (c).
Represents a third embodiment shown in FIGS.
(B) and (c) are dealt with in the order of increasing atomization flow rate (processing amount).

【0019】以下に、この図15をも参照しつつ順次説
明する。
Hereinafter, the description will be sequentially made with reference to FIG.

【0020】図16〜19に示す第1実施例において、
円板A20には4個の貫通孔22が横直径線XX及び縦
直径線YYに対し高さh及び幅mをもって対称に設けら
れ、これらを結ぶH形の直線状溝23が設けられている
(図16参照)。円板B21には、高さhで若干大径の
2個の貫通孔24と、若干幅広でこれらを結ぶ1本の直
線状(Iの字)溝25が縦直径線YYに沿って設けられ
ている(図18参照)。そして位置決め用の穴26を基
準に、円板A,Bを重ねると、2個の貫通孔24が4個
の貫通孔22の中間に位置して重なることはなく、しか
も溝25が溝23とは1個の交差点Kで交差し、これら
が連通するものとなっている。
In the first embodiment shown in FIGS.
The disk A20 is provided with four through holes 22 symmetrically with a height h and a width m with respect to the horizontal diameter line XX and the vertical diameter line YY, and an H-shaped linear groove 23 connecting these is provided. (See FIG. 16). The disk B21 is provided with two through holes 24 having a height h and a slightly larger diameter, and a single linear (I-shaped) groove 25 which is slightly wider and connects these holes along the longitudinal diameter line YY. (See FIG. 18). When the disks A and B are overlapped with each other with the positioning hole 26 as a reference, the two through holes 24 are positioned in the middle of the four through holes 22 and do not overlap each other, and the groove 25 and the groove 23 are not overlapped. Intersect with each other at one intersection K, and they communicate with each other.

【0021】次に、図20〜23に示す第2実施例にお
いては、円板A20の貫通孔22及び円板B21の貫通
孔24の数は第1実施例のものと同じであるが、配置の
高さH、孔径が夫々大きくなっており、そして、これら
を結ぶ溝23、溝25も共に幅広のものとなっている。
しかも、円板A20の溝23は横線が5本となってお
り、これにより円板B21の溝25と交差する交差点K
も5個となっているものである。これらにより第2実施
例のものは第1実施例より流量増大に対処できるもので
ある。
Next, in the second embodiment shown in FIGS. 20 to 23, the numbers of the through holes 22 of the disk A20 and the through holes 24 of the disk B21 are the same as those of the first embodiment, but the arrangement is changed. The height H and the hole diameter are increased, and the groove 23 and the groove 25 that connect them are also wide.
Moreover, the groove 23 of the disk A20 has five horizontal lines, which allows the intersection K to intersect with the groove 25 of the disk B21.
Is also 5 pieces. As a result, the second embodiment can cope with an increase in the flow rate as compared with the first embodiment.

【0022】更に、図24〜27に示す第3実施例にお
いては、円板A20では貫通孔22は孔径が第2実施例
のものより小さいが、その数が6個となっていて、円板
B21では貫通孔24の数が4個となって夫々2個増加
している。これらは共に高さH、幅mでもって配置され
るが、勿論、両方の貫通孔同士は重ならないようになっ
ている。そして上方の位置決め用の穴26を基準に円板
A,Bを重ねると、溝23と溝25の交差点Kは、図2
4に示すように、10本の横線により、計10個とな
り、これにより更なる流量増大に対処できるものであ
る。
Further, in the third embodiment shown in FIGS. 24 to 27, in the disk A20, the through holes 22 have a hole diameter smaller than that of the second embodiment, but the number is six, and the disk In B21, the number of the through holes 24 is four, which is two each. Both of them are arranged with a height H and a width m, but of course, both through holes do not overlap each other. When the disks A and B are overlapped with each other with the upper positioning hole 26 as a reference, the intersection K between the groove 23 and the groove 25 is shown in FIG.
As shown in FIG. 4, ten horizontal lines make a total of ten, which makes it possible to cope with a further increase in the flow rate.

【0023】[0023]

【発明の効果】以上に説明してきたように、本発明によ
れば、物質の微粒化に際し、各業界による各種物質につ
いて要望される粒径分布や所望される処理量の増大等多
様な微粒化要求に的確に対処できる融通性良好で、しか
も、経済的優位性を保障する物質の微粒化装置を提供で
きるものである。
As described above, according to the present invention, when atomizing a substance, various atomizations such as a desired particle size distribution of various substances by each industry and an increase in a desired treatment amount can be achieved. It is possible to provide a fine atomizer for a substance that has a high degree of flexibility and can accurately meet the requirements, and that ensures an economic superiority.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明による装置全体のシステム図である。FIG. 1 is a system diagram of the entire apparatus according to the present invention.

【図2】図1の装置本体の縦断面図である。FIG. 2 is a vertical cross-sectional view of the apparatus body of FIG.

【図3】本発明による第1の実施態様における第1実施
例を示す一対の円板の模式的斜視図である。
FIG. 3 is a schematic perspective view of a pair of discs showing a first example of the first embodiment according to the present invention.

【図4】図3における円板Aの合わせ面P面の正面図で
ある。
4 is a front view of a mating surface P surface of the disk A in FIG.

【図5】図4のV−V線による断面図である。5 is a cross-sectional view taken along the line VV of FIG.

【図6】図3における円板Bの合わせ面P面の正面図で
ある。
FIG. 6 is a front view of a mating surface P surface of the disc B in FIG.

【図7】図6の側面図である。FIG. 7 is a side view of FIG.

【図8】本発明による第1の実施態様における第2実施
例であって、円板Aの合わせ面P面の正面図である。
FIG. 8 is a front view of the mating surface P surface of the disk A, which is a second embodiment of the first embodiment according to the present invention.

【図9】図8のIX−IX線による断面図である。9 is a sectional view taken along line IX-IX in FIG.

【図10】図8に対応する円板Bの合わせ面P面の正面
図である。
10 is a front view of a mating surface P surface of the disc B corresponding to FIG.

【図11】本発明による第1の実施態様における第3実
施例であって、円板Aの合わせ面P面の正面図である。
FIG. 11 is a front view of the mating surface P surface of the disk A, which is the third embodiment of the first mode of the present invention.

【図12】図11のXII−XII線による断面図である。12 is a sectional view taken along line XII-XII in FIG.

【図13】図11に対応する円板Bの合わせ面P面の正
面図である。
13 is a front view of a mating surface P surface of the disc B corresponding to FIG.

【図14】図13のXIV−XIV線による断面図である。14 is a sectional view taken along line XIV-XIV in FIG.

【図15】本発明による第2の実施態様における第1〜
第3実施例のものを一括して示す一対の円板の模式的斜
視図である。
FIG. 15 is a first to a second embodiment of the present invention.
It is a schematic perspective view of a pair of discs collectively showing the thing of 3rd Example.

【図16】図15の(a)第1実施例における円板Aの
合わせ面P面の正面図である。
16 (a) is a front view of a mating surface P surface of the disk A in the first embodiment of FIG.

【図17】図16のXVII−XVII線による断面図である。17 is a sectional view taken along line XVII-XVII in FIG.

【図18】図15の(a)第1実施例における円板Bの
合わせ面P面の正面図である。
FIG. 18 (a) is a front view of the mating surface P of the disc B in (a) the first embodiment.

【図19】図18のXIX−XIX線による断面図である。19 is a sectional view taken along line XIX-XIX in FIG.

【図20】図15の(b)第2実施例における円板Aの
合わせ面P面の正面図である。
20 is a front view of a mating surface P surface of the disk A in the second embodiment of FIG. 15 (b).

【図21】図20のXXI−XXI線による断面図である。21 is a sectional view taken along line XXI-XXI of FIG.

【図22】図15の(b)第2実施例における円板Bの
合わせ面P面の正面図である。
22 (b) is a front view of the mating surface P of the disc B in (b) the second embodiment. FIG.

【図23】図22のXXIII−XXIII線による断面図であ
る。
23 is a sectional view taken along line XXIII-XXIII in FIG.

【図24】図15の(c)第3実施例における円板Aの
合わせ面P面の正面図である。
FIG. 24 is a front view of a mating surface P surface of the disk A in the third embodiment (c) of FIG.

【図25】図24のXXV―XXV線による断面図である。25 is a sectional view taken along line XXV-XXV in FIG.

【図26】図15の(c)第3実施例における円板Bの
合わせ面P面の正面図である。
FIG. 26 is a front view of the mating surface P surface of the disk B in the third embodiment of FIG. 15 (c).

【図27】図26のXXVII−XXVII線による断面図であ
る。
27 is a sectional view taken along line XXVII-XXVII in FIG.

【符号の説明】[Explanation of symbols]

1…原料供給口 2…高圧ポンプ 3…本体 4…微粒化製品の受入器 5…円筒体 6…円筒 7…円筒 8…ボルト 9…ピン 10…円板A 11…円板B 12…貫通孔 13…溝 14…貫通孔 15…位置決め用の穴 20…円板A 21…円板B 22…貫通孔 23…溝 24…貫通孔 25…溝 26…位置決め用の穴 P…合わせ面 XX…横直径線 YY…縦直径線 K…交差点 1 ... Raw material supply port 2 ... High-pressure pump 3 ... Main body 4 ... Receptor for atomized products 5 ... Cylindrical body 6 ... Cylinder 7 ... Cylinder 8 ... bolt 9 ... pin 10 ... Disc A 11 ... Disc B 12 ... Through hole 13 ... Groove 14 ... Through hole 15 ... Positioning hole 20 ... Disc A 21 ... Disc B 22 ... Through hole 23 ... Groove 24 ... Through hole 25 ... Groove 26 ... Positioning hole P ... Mating surface XX ... Horizontal diameter line YY ... vertical diameter line K ... intersection

───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 吉延 東京都中央区京橋1−17−4 松永ビル5 F エス・ジーエンジニアリング株式会社 内 (72)発明者 高橋 幸悦 愛知県名古屋市熱田区桜田町3−13 吉田 機械興業株式会社内 (72)発明者 大村 康 愛知県名古屋市熱田区桜田町3−13 吉田 機械興業株式会社内 Fターム(参考) 4G035 AB40 AC26 AE13    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Yoshinobu Hattori             1-17-4 Kyobashi, Chuo-ku, Tokyo Matsunaga Building 5             F G Engineering Co., Ltd.             Within (72) Inventor Koetsu Takahashi             Yoshida, 3-13 Sakurada-cho, Atsuta-ku, Nagoya-shi, Aichi             Machinery Industry Co., Ltd. (72) Inventor Yasushi Omura             Yoshida, 3-13 Sakurada-cho, Atsuta-ku, Nagoya-shi, Aichi             Machinery Industry Co., Ltd. F-term (reference) 4G035 AB40 AC26 AE13

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 原料供給口に供給される原料を加圧して
本体に送り、この本体で前記原料中の物質を微粒化して
取出す物質の微粒化装置において、前記本体は、入口及
び出口付きの円筒体と、この円筒体に位置合わせされ面
一にP面にて重ねられ組込まれる一対の円板A,Bを有
し、該円板A,Bには互いに反対側の半円部に2個の貫
通孔が夫々設けられ、また、該円板A,Bのいずれか一
方のP面には当該一方の2個の貫通孔と接続し、かつ、
横直径線XX及び縦直径線YYに対し対称な所定の形状
の溝が設けられており、円板A,BをP面で重ねたと
き、前記溝の両端部が他方の2個の貫通孔に連通するよ
うになっていることを特徴とする物質の微粒化装置。
1. A material atomizer for pressurizing a raw material supplied to a raw material supply port and sending it to a main body, and atomizing the substance in the raw material by this main body, wherein the main body has an inlet and an outlet. It has a cylindrical body and a pair of discs A and B which are aligned with the cylindrical body and are flush with each other and assembled on the P plane, and the discs A and B have two semicircular portions on opposite sides. Through holes are provided respectively, and the P surface of either one of the disks A and B is connected to the two through holes of the one, and
A groove having a predetermined shape symmetrical to the horizontal diameter line XX and the vertical diameter line YY is provided, and when the disks A and B are overlapped with each other on the P plane, the two ends of the groove are the other two through holes. A device for atomizing a substance, which is characterized in that it is connected to
【請求項2】 原料供給口に供給される原料を加圧して
本体に送り、この本体で前記原料中の物質を微粒化して
取出す物質の微粒化装置において、前記本体は、入口及
び出口付きの円筒体と、この円筒体に位置合わせされ面
一にP面にて重ねられ組込まれる一対の円板A,Bを有
し、該円板A,Bは横直径線XX及び縦直径線YYに対
して対称にかつ互いに重ならない位置に2〜6個の貫通
孔を有してこれらの貫通孔がP面において夫々の円板の
P面に設けられた直線状の溝により接続しており、円板
A,BをP面で重ねたとき前記両方の溝が1〜5個の交
差点Kで交差することにより互いに連通するようになっ
ていることを特徴とする物質の微粒化装置。
2. A material atomizer for pressurizing a raw material supplied to a raw material supply port to send it to a main body, and atomizing the substance in the raw material by this main body, wherein the main body has an inlet and an outlet. It has a cylindrical body and a pair of discs A and B which are aligned with the cylindrical body and are superposed on the P plane so as to be integrated with each other. The discs A and B are arranged on a lateral diameter line XX and a longitudinal diameter line YY. Two to six through holes are provided symmetrically with respect to each other and at positions not overlapping with each other, and these through holes are connected to each other by a linear groove provided on the P surface of each disk on the P surface, A device for atomizing a substance, characterized in that, when the disks A and B are overlapped with each other on a P plane, the both grooves are communicated with each other by intersecting at 1 to 5 intersections K.
JP2001203318A 2001-07-04 2001-07-04 Substance atomizer Expired - Fee Related JP3696808B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001203318A JP3696808B2 (en) 2001-07-04 2001-07-04 Substance atomizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001203318A JP3696808B2 (en) 2001-07-04 2001-07-04 Substance atomizer

Publications (2)

Publication Number Publication Date
JP2003010663A true JP2003010663A (en) 2003-01-14
JP3696808B2 JP3696808B2 (en) 2005-09-21

Family

ID=19039980

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3696808B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7789108B1 (en) * 2006-11-20 2010-09-07 Aeromed Technologies Llc Micro-flow fluid restrictor, pressure spike attenuator, and fluid mixer
EP2682518A2 (en) 2012-07-03 2014-01-08 Showa Denko K.K. Method for producing composite carbon fibers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7789108B1 (en) * 2006-11-20 2010-09-07 Aeromed Technologies Llc Micro-flow fluid restrictor, pressure spike attenuator, and fluid mixer
EP2682518A2 (en) 2012-07-03 2014-01-08 Showa Denko K.K. Method for producing composite carbon fibers

Also Published As

Publication number Publication date
JP3696808B2 (en) 2005-09-21

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