JP2012166168A - Solid material crusher - Google Patents
Solid material crusher Download PDFInfo
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- JP2012166168A JP2012166168A JP2011030561A JP2011030561A JP2012166168A JP 2012166168 A JP2012166168 A JP 2012166168A JP 2011030561 A JP2011030561 A JP 2011030561A JP 2011030561 A JP2011030561 A JP 2011030561A JP 2012166168 A JP2012166168 A JP 2012166168A
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- floating cylinder
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- crushed
- floating
- cylinder
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Abstract
Description
本発明は、固形物を粉砕する装置に関するものである。 The present invention relates to an apparatus for pulverizing a solid material.
従来の粉砕機では磨り潰しや押し潰しに拠る物が多く、粉砕過程の中で発生する熱等の様々な原因によって原料の変質が起こっている。
また、従来の粉砕機は複雑な構造をしていて、メンテナンス性が悪い上に食品等を扱う場合等で、衛生上問題がある。
In conventional pulverizers, there are many things that depend on crushing or crushing, and the raw materials are altered due to various causes such as heat generated in the pulverization process.
Further, the conventional pulverizer has a complicated structure, has poor maintainability and has a sanitary problem when handling foods and the like.
出願人は、この様な実状に鑑みて、原料の変質を極力無くし、様々な固形物を粉砕する事が出来、簡単な構造でメンテナンス性に優れ、粒度の選定が可能な粉砕機の創作に至った。 In light of this situation, the applicant is able to create a pulverizer that can reduce the quality of raw materials as much as possible, pulverize various solids, has a simple structure, is easy to maintain, and can select the particle size. It came.
この様な粉砕機の場合、粒度の選別の為にスクリーンやメッシュなどを有しており複雑な構造をしている物が殆どであり、メンテナンス性や食品等を扱う場合において衛生上問題があり、粉砕過程で発生する熱が外に逃げにくいものが多い。また、この様な構造の粉砕機の場合、構造が複雑な事で熱が外に逃げにくい物が多い。本発明は上記問題点に鑑み、スクリーンやメッシュなどを装備することなく、メンテナンス性に優れ洗浄しやすく衛生上にも問題無く、簡単な構造で熱を外に逃がし易くし、粒度の選定が可能な粉砕機を提供することを技術的課題とする。 In the case of such a pulverizer, most of them have a complicated structure with a screen or mesh for selecting the particle size, and there are hygiene problems when handling maintenance and foods. In many cases, heat generated during the grinding process is difficult to escape. In addition, in the case of a pulverizer having such a structure, there are many things in which heat is difficult to escape due to the complicated structure. In view of the above-mentioned problems, the present invention is not equipped with a screen, mesh, etc., has excellent maintainability, is easy to clean and has no sanitary problems, and has a simple structure that allows heat to escape to the outside, allowing selection of particle size. Technical problem is to provide a simple grinder.
上記課題を解決するため、原料を供給する供給装置と供給装置下方供給口に配設されると供に、外周縁に翼板を放射状に複数枚取り付けてあり、駆動モーターの動力によって回転する回転翼板と、回転翼板を収める丸型ケースで構成した、という技術的手段を講じるものである。 In order to solve the above-mentioned problem, a rotation device is provided with a plurality of blades radially attached to the outer peripheral edge and rotated by the power of the drive motor, in addition to being arranged in a supply device for supplying raw materials and a supply device lower supply port The technical means is composed of a wing plate and a round case that houses the rotating wing plate.
この様に、極簡単な構成であるので、メンテナンス性の良否と食品等を扱う場合においての衛生上の問題とを解決するものである。 In this way, since it has an extremely simple configuration, it solves the quality of maintenance and the sanitary problem when handling foods and the like.
また、回転翼板で発生する排気流によって浮遊筒に浮遊する被粉砕物を集粉するという簡単な構成によってメンテナンス性の良否と衛生上の問題と粒度の選定方法の問題を解決するものである。 In addition, the simple structure of collecting the pulverized material floating in the floating cylinder by the exhaust flow generated by the rotor blades solves the problem of quality of maintenance, hygiene problems, and particle size selection method. .
また、丸型ケースの前面を開閉する事ができ、このことによってメンテナンス性の良否と衛生上の問題とを解決するものである。 In addition, the front surface of the round case can be opened and closed, and this solves the quality of maintenance and the sanitary problem.
また、回転翼板による排気流と送風機の風によって熱を逃がす事で原料の変質を抑える。 In addition, the heat is released by the exhaust flow from the rotor blades and the wind of the blower, thereby suppressing the deterioration of the raw material.
本発明の固形物粉砕機は、米粉や大豆粉や小麦粉など製造過程での熱による変質を抑えて、風味の良い粉を作れるという利点がある。 The solid material pulverizer of the present invention has an advantage that it can produce a savory powder while suppressing deterioration due to heat in the production process such as rice flour, soybean flour, and wheat flour.
また、構成が簡単な事でメンテナンスや清掃が簡易であり、食品を扱う場合に衛生面で利点がある。 In addition, since the structure is simple, maintenance and cleaning are simple, and there is an advantage in terms of hygiene when handling food.
以下、本発明を実施するための形態を説明する。図1は固形物粉砕機の正面及び粉砕部と浮遊筒の断面図である。図2は固形物粉砕機の側面及び供給装置部と粉砕部の断面図である。図3は固形物粉砕機の粉砕部の正面外形図である。図4は固形物粉砕機の粉砕部の側面外形図である。 Hereinafter, modes for carrying out the present invention will be described. FIG. 1 is a cross-sectional view of the front surface of the solid material pulverizer and the pulverization section and the floating cylinder. FIG. 2 is a side view of the solid material pulverizer, and a cross-sectional view of the supply device section and the pulverization section. FIG. 3 is a front external view of the pulverizing part of the solid pulverizer. FIG. 4 is a side view of the pulverizing part of the solid pulverizer.
丸型ケース8は円形面を略垂直にして基台16に溶接で固定され、設置される。また、丸型ケース8には供給管7が背面の適当な位置に溶接で取り付けられる。供給管7の上部には、図示しない駆動モーターによって回転するローター供給機6が溶接で取り付けられている。 The round case 8 is fixed by welding to the base 16 with the circular surface substantially vertical, and is installed. Further, the supply pipe 7 is attached to the round case 8 by welding at an appropriate position on the back surface. A rotor feeder 6 that is rotated by a drive motor (not shown) is attached to the upper portion of the supply pipe 7 by welding.
ローター供給機6には原材料投入用の供給ホッパ5を上部に取り付けてある。 A supply hopper 5 for charging raw materials is attached to the upper portion of the rotor feeder 6.
丸型閉止蓋13は丸型ケース8に開閉用ヒンジ14によって開閉できる様に支持され、溶接で取り付けてある。また、丸型ケース8と丸型閉止蓋13は図示しないファスナーやクランプなどの締め付け器具で閉止される。また、丸型閉止蓋13には、図示しない吸気量調整用のバルブまたはダンパー等をそなえた吸気管10を溶接によって取り付けられている。 The round closure lid 13 is supported by the round case 8 so as to be opened and closed by an opening and closing hinge 14 and is attached by welding. The round case 8 and the round closure lid 13 are closed by a fastening device such as a fastener or a clamp (not shown). In addition, an intake pipe 10 having an intake air amount adjusting valve or a damper (not shown) is attached to the round closing lid 13 by welding.
回転翼板1は円形であり、丸型ケース8の内径に対して90%程度の直径である。また、回転翼板1には丸型ケース直径の15パーセント程度の辺長で出来た四角型の翼板2を排気流を発生させる為に放射線に対して角度をつけ、複数枚を等間隔で外周へ丸型ケース8の内面との間に数ミリの隙間をあけ、回転翼板1に対して垂直に溶接で取り付けてある。また、回転翼板1には回転主軸3を回転翼板1に対して垂直に回転翼板1の円の中心へ溶接またはボルト・ナットで取り付けてある。 The rotary blade 1 is circular and has a diameter of about 90% with respect to the inner diameter of the round case 8. In addition, the rotary vane 1 has a square vane plate 2 having a side length of about 15% of the diameter of the round case. The rotary vane plate 1 is angled with respect to the radiation in order to generate an exhaust flow, and a plurality of the vane blades are equally spaced. A gap of several millimeters is formed between the outer periphery and the inner surface of the round case 8 and is attached to the rotor blade 1 by welding. Further, the rotary blade 1 is attached with a rotating main shaft 3 perpendicularly to the rotary blade 1 by welding or bolts and nuts to the center of the circle of the rotary blade 1.
回転主軸3は丸型ケース8の背面の中心を貫通しており、駆動モーター4と図示しないチェーン等で連結され、図示しないベアリングユニットで支持されている。 The rotation main shaft 3 passes through the center of the back surface of the round case 8 and is connected to the drive motor 4 by a chain (not shown) and supported by a bearing unit (not shown).
浮遊筒a9と浮遊筒b18と連結短管12はボルト・ナットで連結され、丸型ケース8の上半円外周に略垂直上向き方向で排出管17にボルト・ナットで取り付けられる。また、浮遊筒b18を交換し、浮遊筒9及び浮遊筒18で構成される浮遊筒の全長を変えることができる。 The floating cylinder a9, the floating cylinder b18, and the connecting short pipe 12 are connected by bolts and nuts, and are attached to the discharge pipe 17 by bolts and nuts in an approximately vertical upward direction on the outer circumference of the upper half circle of the round case 8. Moreover, the floating cylinder b18 can be replaced | exchanged and the full length of the floating cylinder comprised by the floating cylinder 9 and the floating cylinder 18 can be changed.
浮遊筒9の最上部には被粉砕物排出口11が設置される。 A pulverized material discharge port 11 is installed at the top of the floating cylinder 9.
浮遊筒排出口11後段には、図示しないサイクロンや集塵機などの集粉機器と、浮遊筒に負圧を与えるブロワー等の送風機器が取り付けられる。 At the rear stage of the floating cylinder discharge port 11, a powder collecting device such as a cyclone or a dust collector (not shown) and a blower device such as a blower for applying a negative pressure to the floating cylinder are attached.
次に、本発明の固形物粉砕機の作用を説明する。供給ホッパ5に投入された固形物は図示しない駆動モーターによって回転するローター供給機6によって供給管7を通って粉砕部へ投入される。駆動モーター4の動力が図示しないベアリングユニットによって支持される回転主軸3によって伝達され翼板2を配設された回転翼板1を丸型ケース8と丸型閉止蓋13で構成される空間の内部で回転し、その回転によって、前述の供給装置によって供給された固形物はランダムに丸型ケース8内にたたきつけられ被粉砕物にされる。被粉砕物は回転翼板8と翼板2によって発生する排気流で丸型ケース8の上半円外周の略垂直上向きに配置された浮遊筒9の内部へ浮遊される。この時、未被粉砕のものは自重によって粉砕部へ戻り更に粉砕され、細かく粉砕された被粉砕物だけが浮遊筒最上部へと浮遊する。浮遊筒最上部に浮遊された被粉砕物は浮遊筒の最上部に配設してある浮遊筒排出口11から図示しない送風機の負圧によって排出される。排出された被粉砕物は図示しないサイクロンや集塵機等の集粉装置によって集粉される。 Next, the operation of the solid matter pulverizer of the present invention will be described. The solid matter put into the supply hopper 5 is put into the pulverizing section through the supply pipe 7 by the rotor feeder 6 rotated by a drive motor (not shown). The power of the drive motor 4 is transmitted by a rotary main shaft 3 supported by a bearing unit (not shown), and the rotary vane plate 1 on which the vane plate 2 is disposed is placed inside a space constituted by a round case 8 and a round closure lid 13. By the rotation, the solid material supplied by the above-described supply device is randomly beaten in the round case 8 to be crushed. The object to be crushed is floated in the floating cylinder 9 arranged substantially vertically upward on the outer circumference of the upper half circle of the round case 8 by the exhaust flow generated by the rotary blade 8 and the blade 2. At this time, the unground material is returned to the pulverizing part by its own weight and further pulverized, and only the finely pulverized material floats to the top of the floating cylinder. The object to be crushed suspended at the top of the floating cylinder is discharged from the floating cylinder discharge port 11 provided at the top of the floating cylinder by the negative pressure of a blower (not shown). The discharged material to be crushed is collected by a powder collecting device such as a cyclone or a dust collector (not shown).
浮遊筒は前述のとおり、全長を変えることができ、全長を長くした場合にはより細かい粒度に粉砕された被粉砕物だけが浮遊筒最上部に浮遊し、全長を短くした場合には粗い粒度の被粉砕物も浮遊筒最上部に浮遊し、これを集粉機器で集粉する事に因り、浮遊筒の長さで粒度の調整し、選別して集粉することができる。 As described above, the floating cylinder can be changed in total length. When the total length is increased, only the material to be crushed to a finer particle size floats at the top of the floating cylinder, and when the total length is shortened, the coarse particle size is increased. The material to be crushed also floats on the top of the floating cylinder and is collected by a powder collecting device, so that the particle size can be adjusted by the length of the floating cylinder, and can be selected and collected.
また、吸気管10に取り付けられた図示しないバルブやダンパー等による吸気流量調整や、浮遊筒排出口11の後段に取り付けられた図示しない送風機器の排気流量調整に因っても浮遊筒最上部に浮遊する被粉砕物の粒度を調整し、選別して集粉することができる。 In addition, the intake air flow rate is adjusted by a valve or a damper (not shown) attached to the intake pipe 10 and the exhaust gas flow rate adjustment of a blower (not shown) attached at the subsequent stage of the floating tube discharge port 11 is placed at the top of the floating cylinder. It is possible to adjust the particle size of the floating object to be crushed and to select and collect the powder.
米や大豆や小麦等の穀物類を粉砕し、粒度の揃った粉を製造できる。 Grains such as rice, soybeans and wheat can be pulverized to produce powders of uniform particle size.
1 回転翼板
2 翼板
3 回転主軸
4 駆動モーター
5 供給ホッパ
6 ローター供給機
7 供給管
8 丸型ケース
9 浮遊筒a
10 吸気管
11 浮遊筒排出口
12 連結短管
13 丸型閉止蓋
14 開閉用ヒンジ
15 取手
16 基台
17 排出管
18 浮遊筒b
DESCRIPTION OF SYMBOLS 1 Rotating blade 2 Blade 3 Rotating spindle 4 Drive motor 5 Supply hopper 6 Rotor feeder 7 Supply pipe 8 Round case 9 Floating cylinder a
DESCRIPTION OF SYMBOLS 10 Intake pipe 11 Floating cylinder discharge port 12 Short connection pipe 13 Round closure lid 14 Opening and closing hinge 15 Handle 16 Base 17 Discharge pipe 18 Floating cylinder b
Claims (3)
The particle size of the crushed material that reaches the top of the floating cylinder can be adjusted by changing or extending the floating cylinder. Moreover, the particle size of the material to be crushed that reaches the top of the floating cylinder can be adjusted by adjusting the negative pressure flow rate when collecting powder from the floating cylinder. Furthermore, the particle size adjustment method characterized by being able to adjust the particle size of the material to be crushed to reach the top of the floating cylinder by adjusting the flow rate of the intake air flow sucked into the pulverization unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011030561A JP2012166168A (en) | 2011-02-16 | 2011-02-16 | Solid material crusher |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2011030561A JP2012166168A (en) | 2011-02-16 | 2011-02-16 | Solid material crusher |
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Publication Number | Publication Date |
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JP2012166168A true JP2012166168A (en) | 2012-09-06 |
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ID=46970868
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2011030561A Withdrawn JP2012166168A (en) | 2011-02-16 | 2011-02-16 | Solid material crusher |
Country Status (1)
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JP (1) | JP2012166168A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016129866A (en) * | 2015-01-13 | 2016-07-21 | 日本コークス工業株式会社 | Dry type medium agitation pulverizer, and operational method therefor |
US10481257B2 (en) | 2014-10-30 | 2019-11-19 | Mitsubishi Electric Corporation | Synthetic aperture radar apparatus |
WO2021161445A1 (en) * | 2020-02-13 | 2021-08-19 | 株式会社アサヒ | Glass crushing equipment |
-
2011
- 2011-02-16 JP JP2011030561A patent/JP2012166168A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10481257B2 (en) | 2014-10-30 | 2019-11-19 | Mitsubishi Electric Corporation | Synthetic aperture radar apparatus |
JP2016129866A (en) * | 2015-01-13 | 2016-07-21 | 日本コークス工業株式会社 | Dry type medium agitation pulverizer, and operational method therefor |
WO2021161445A1 (en) * | 2020-02-13 | 2021-08-19 | 株式会社アサヒ | Glass crushing equipment |
JPWO2021161445A1 (en) * | 2020-02-13 | 2021-08-19 | ||
JP7121417B2 (en) | 2020-02-13 | 2022-08-18 | 株式会社アサヒ | glass crusher |
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Date | Code | Title | Description |
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A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20140513 |