Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6333898B2 - - Google Patents
[go: Go Back, main page]

JPS6333898B2 - - Google Patents

Info

Publication number
JPS6333898B2
JPS6333898B2 JP55133891A JP13389180A JPS6333898B2 JP S6333898 B2 JPS6333898 B2 JP S6333898B2 JP 55133891 A JP55133891 A JP 55133891A JP 13389180 A JP13389180 A JP 13389180A JP S6333898 B2 JPS6333898 B2 JP S6333898B2
Authority
JP
Japan
Prior art keywords
stirring
container
outlet
impeller
action
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.)
Expired
Application number
JP55133891A
Other languages
Japanese (ja)
Other versions
JPS5759622A (en
Inventor
Akio Tanaka
Juzo Itakura
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.)
HOSOKAWA MIKURON KK
Original Assignee
HOSOKAWA MIKURON KK
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 HOSOKAWA MIKURON KK filed Critical HOSOKAWA MIKURON KK
Priority to JP55133891A priority Critical patent/JPS5759622A/en
Publication of JPS5759622A publication Critical patent/JPS5759622A/en
Publication of JPS6333898B2 publication Critical patent/JPS6333898B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/53Mixing liquids with solids using driven stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75Discharge mechanisms
    • B01F35/754Discharge mechanisms characterised by the means for discharging the components from the mixer
    • B01F35/7547Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】 この発明は粉粒体を対象とした撹拌装置に関す
るもので、たとえば混合、乾燥工程などに広く利
用されるものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a stirring device for powder and granular materials, and is widely used in, for example, mixing and drying processes.

従来、この種の撹拌装置は種々提案されている
が物性、形態の変化がきわめて大きい粉粒体、あ
るいはその湿潤物質の場合、これら装置の運転操
作には困難な事態になることがよく起る。たとえ
ば、軸心が水平に設置された円筒形容器内に回転
撹拌羽根車によつて撹拌と同時に入口から出口に
向つて被処理材料(以下単に原料という)を移送
させ、順次出口より適量づつ排出させ、かつ器内
においては当該処理に必要な分量の原料を滞留さ
せ所定の操作、たとえば混合、乾燥などを行わせ
るが、撹拌作用と移送作用を適度に組み合わせ所
期の目的を達成させることは実際上はなはだ難か
しく、また単一の撹拌機構だけでは充分満足され
る撹拌効果は得られない。この発明は、前述のよ
うな軸心が水平に設置された円筒形容器に回転撹
拌羽根車を内蔵する粉粒体の撹拌装置において、
主たる撹拌作用と共に移送作用と副撹拌作用を効
果的に複合させたものとして、前述の問題を解決
することを目的とする。
Various stirring devices of this type have been proposed in the past, but it is often difficult to operate these devices in the case of powder or granular materials whose physical properties and shapes change significantly, or their wet materials. . For example, the material to be processed (hereinafter simply referred to as raw material) is stirred by a rotating stirring impeller into a cylindrical container whose axis is set horizontally, and is simultaneously transferred from the inlet to the outlet, and the appropriate amount is sequentially discharged from the outlet. The necessary amount of raw materials for the treatment is retained in the vessel and predetermined operations such as mixing and drying are performed, but it is impossible to achieve the desired purpose by appropriately combining the stirring action and the transport action. In practice, this is extremely difficult, and a sufficiently satisfactory stirring effect cannot be obtained with a single stirring mechanism alone. The present invention provides a stirring device for powder and granular material, which includes a rotary stirring impeller built into a cylindrical container whose axis is horizontally installed as described above.
The purpose is to solve the above-mentioned problems by effectively combining the main stirring action, the transfer action, and the sub-stirring action.

次にこの発明の構成は回転する撹拌羽根車を内
蔵する軸心方向がほゞ水平に設置される容器の一
端に入口、他端に出口を有し、前記撹拌羽根車の
撹拌要素は容器の内周壁に沿つて回転外側部位に
撹拌羽根車の軸心方向に平行な撹拌面を有する主
撹拌羽根群と、該主撹拌羽根群の内側に位置し
て、前記容器の軸心方向に対し傾斜した送り面を
有することが出来る小片状の副撹拌羽根群を具備
し、前記出口は前記容器の壁面にあつて該容器の
軸心とほゞ同じ高さ付近に設け、かつ、前記出口
はその開口断面の下辺の水平高さが上下方向に調
節可能にしたものである。
Next, the configuration of the present invention has an inlet at one end and an outlet at the other end of a container with a built-in rotating stirring impeller installed so that its axial direction is substantially horizontal, and the stirring element of the stirring impeller is connected to the container. a main stirring blade group having a stirring surface parallel to the axial direction of the stirring impeller on the outer side of the rotation along the inner peripheral wall; and a main stirring blade group located inside the main stirring blade group and inclined with respect to the axial direction of the container. a group of sub-agitating blades in the form of small pieces that can have a feeding surface such that the outlet is provided on the wall surface of the container at approximately the same height as the axis of the container; The horizontal height of the lower side of the opening cross section can be adjusted in the vertical direction.

次にこの発明の実施例について述べる。軸心が
水平に配置された容器2の両端部には軸受9が設
けられ撹拌羽根車1の軸10を回転可能に支受
し、軸10の一端にはチエンホイール11が固着
され、図示省略のモータ、およびチエンにより回
転駆動される。容器2の一側には原料の入口3が
設けられ、図示省略の原料供給装置、あるいは前
工程の出口に接続されており、他側には容器2の
内壁下面より軸心までのとほぼ同じ高さに開口断
面aを有する出口4が設けられ、前記開口断面a
の下辺bの高さhは上下方向に調節可能とされて
いる。すなわち、堰板12に設けられたネジ13
と、出口4にその軸方向の移動を規制したネジ棒
14で、ハンドル40を回転させ、堰板12を上
下動させることにより行われる。撹拌羽根車1の
撹拌要素5は、容器2の内周壁6に沿つた回転外
側部位に、撹拌羽根車1の軸心方向に平行な撹拌
面Eを有する主撹拌羽根7群と、該主撹拌羽根7
群の内側に、たとえば前記撹拌羽根車1の回転に
よつて入口3から出口4の方向に向つて移送作用
を有するように前記容器2の軸心方向に対し傾斜
した送り面Fを有する小片状の副撹拌羽根8群を
具備している。副撹拌羽根8群は、たとえば前記
主撹拌羽根7群を軸10から支持する杆14に嵌
着させ、あるいは送り面Fの傾斜度合が自在に変
更可能としてもよい。その実施例は、第3図にお
ける副撹拌羽根8に対し、押え板15とボルト1
6でもつて杆14を挾持することによつても可能
である。
Next, embodiments of this invention will be described. Bearings 9 are provided at both ends of the container 2 whose shaft center is horizontally arranged to rotatably support the shaft 10 of the stirring impeller 1, and a chain wheel 11 is fixed to one end of the shaft 10, not shown. It is rotated by a motor and a chain. A raw material inlet 3 is provided on one side of the container 2 and is connected to a raw material supply device (not shown) or an outlet of a previous process, and on the other side there is a raw material inlet 3 that is approximately the same as the one from the lower surface of the inner wall of the container 2 to the axis. An outlet 4 having an opening cross section a at the height is provided, said opening cross section a
The height h of the lower side b is adjustable in the vertical direction. That is, the screws 13 provided on the weir plate 12
This is done by rotating the handle 40 using the threaded rod 14 that restricts the axial movement of the outlet 4 and moving the weir plate 12 up and down. The stirring element 5 of the stirring impeller 1 includes a group of 7 main stirring blades having a stirring surface E parallel to the axial direction of the stirring impeller 1 on the outer side of rotation along the inner circumferential wall 6 of the container 2, and Feather 7
A small piece having, on the inside of the group, a feeding surface F inclined with respect to the axial direction of the container 2 so as to have a transfer action from the inlet 3 toward the outlet 4 by the rotation of the stirring impeller 1, for example. It is equipped with eight groups of sub-stirring blades shaped like the following. The 8 groups of auxiliary stirring blades may be fitted, for example, to a rod 14 that supports the 7 groups of main stirring blades from the shaft 10, or the degree of inclination of the feeding surface F may be freely changeable. In this embodiment, a holding plate 15 and a bolt 1 are used for the sub stirring blade 8 in FIG.
It is also possible to do this by holding the rod 14 with the rod 14.

次に前述実施例における作用効果を述べると、
撹拌羽根車1を回転させておいて、入口3より原
料を供給する。容器2内に供給された材料は撹拌
されながらその滞留量は増し、同時に出口4から
は除々に原料は排出され、堰板12で形成される
開口断面aの下辺bの高さhによつて、前記原料
の供給と排出の状態によつてある一定の平衡状態
が得られ、容器2内に原料の所定の滞留量が得ら
れ、換言すれば所定の撹拌操作時間を与えること
が出来るが、容器2の軸心方向と平向に設けられ
た主撹拌羽根7群の撹拌面Eは原料の入口3から
出口4に向かわせる移送作用は有していないので
原料を撹拌する、という点では効果的、かつ高効
率であるが、前述のように軸方向の移送作用がな
いので容器2内での全体の滞留量は過大になり易
く、このことによる不都合を有していることにな
る。ところがこの発明のように副撹拌羽根8の傾
斜を有する送り面Fによつて滞留量が増加した場
合には移送作用が働くので滞留量の過大は回避さ
れることになる。
Next, the effects of the above-mentioned embodiments will be described.
While the stirring impeller 1 is being rotated, raw materials are supplied from the inlet 3. As the material supplied into the container 2 is stirred, the retention amount thereof increases, and at the same time, the material is gradually discharged from the outlet 4. A certain equilibrium state is obtained depending on the supply and discharge conditions of the raw materials, and a predetermined retention amount of the raw materials can be obtained in the container 2, in other words, a predetermined stirring operation time can be given. The stirring surface E of the group of main stirring blades 7, which is provided parallel to the axial direction of the container 2, does not have the effect of transferring the raw material from the inlet 3 to the outlet 4, so it is effective in stirring the raw material. However, as mentioned above, since there is no axial transfer action, the total amount retained in the container 2 tends to be excessive, which is a disadvantage. However, when the retention amount is increased due to the inclined feeding surface F of the sub-agitation blade 8 as in the present invention, the transfer action works, so that an excessive retention amount is avoided.

また、副撹拌羽根8は前述のように、また図示
のように小片状とし、連続した面、または大きな
面をもたないので動力的には大駆動力を必要とせ
ず、また過大な移送作用を有しないので容器2内
容積を有効に充分活用して撹拌作用を付与させる
ことが出来る。
In addition, as described above and as shown in the figure, the sub-agitation blade 8 is shaped like a small piece and does not have a continuous surface or a large surface, so it does not require a large driving force and does not require excessive transfer. Since it has no action, the internal volume of the container 2 can be effectively and fully utilized to impart a stirring action.

なお、以上の説明は単に混合操作について述べ
たが、撹拌に伴わせ乾燥操作を加える場合は、図
示を省略したが、容器2の外周囲に加熱ジヤケツ
トを付設し、あるいは入口3、出口4よりそれぞ
れ熱気流を導入したり、また、軸10を中空体と
して撹拌羽根車1に機外より熱媒体を取り入れる
ことにより行えばよい。
Although the above explanation has simply been about the mixing operation, if a drying operation is to be added along with the stirring, a heating jacket (not shown) should be attached to the outer periphery of the container 2, or a heating jacket from the inlet 3 and outlet 4 should be added. This can be carried out by introducing a hot air stream or by introducing a heat medium into the stirring impeller 1 from outside by using the shaft 10 as a hollow body.

また、副撹拌羽根8の送り面Fの送り方向は、
かならずしも出口4方向に向う移送作用のみを行
わせることなく、容器2内原料の撹拌状態によつ
ては前述の移送作用とは逆方向に、あるいは送り
作用をもたせない方向、たとえば撹拌要素5の回
転方向と平行に、または同回転方向と直角方向の
面と同じ方向に部分的に設定してもよい。
Furthermore, the feeding direction of the feeding surface F of the sub-agitating blade 8 is as follows:
It is not always necessary to perform the transfer action only in the direction of the outlet 4, but depending on the stirring state of the raw material in the container 2, the rotation of the stirring element 5 may be performed in the opposite direction to the above-mentioned transfer action, or in a direction that does not provide the transfer action, such as the rotation of the stirring element 5. It may be partially set parallel to the rotation direction or in the same direction as a plane perpendicular to the same rotation direction.

いずれにしても、出口4における堰板12の高
さの調節と、前記副撹拌羽根8の送り面Fの角度
調節の関連において機内原料の滞留量を調節する
ことにより所期の目的に沿つた撹拌操作を行わせ
る。なお、17は第2排出口で前述の出口4と共
同で原料を排出したり、最終的に原料を完全排出
したりするときに用いるものであり、排出弁等は
図示省略されている。
In any case, the desired purpose can be achieved by adjusting the amount of raw material retained in the machine by adjusting the height of the weir plate 12 at the outlet 4 and adjusting the angle of the feeding surface F of the sub-agitating blade 8. Perform stirring operation. Reference numeral 17 denotes a second discharge port, which is used to discharge the raw material together with the aforementioned outlet 4 or to finally discharge the raw material completely, and the discharge valve and the like are not shown.

以上のように、本発明によれば、撹拌作用と移
送作用を適度に組み合わせることが容易に出来る
ので容器内原料の滞留量、すなわち撹拌操作時間
の調節がしやすくなること、あるいは撹拌動力の
省力、適正化に役立つほか、容器内原料の過剰な
片寄りとか、これらにともなう機械的な折損事故
等の有効な防止対策にもなる。また副撹拌羽根は
小片状で連続移送面をもたないので小きざみの、
かつ数多の撹拌作用と解砕作用を同時に付与する
ことになるので主撹拌羽根群の撹拌作用と複合さ
れ、能率の高い撹拌作用を付加することが出来、
このことは単に前述撹拌作用のみならず、乾燥操
作を行わせる場合、きわめて効果的であるなど、
工業上有用なものである。
As described above, according to the present invention, it is possible to easily combine the stirring action and the transfer action in an appropriate manner, which makes it easier to adjust the amount of raw material retained in the container, that is, the stirring operation time, or to save on stirring power. In addition to being useful for optimization, it is also an effective preventive measure against excessive skewing of raw materials in containers and mechanical breakage accidents caused by these. In addition, the sub-stirring blades are in the form of small pieces and do not have a continuous transfer surface, so they can be
In addition, since multiple stirring actions and crushing actions are applied at the same time, it is combined with the stirring action of the main stirring blade group, and a highly efficient stirring action can be added.
This is extremely effective not only for the above-mentioned stirring action but also for drying operations.
It is industrially useful.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の実施例を示す主要断面図、
第2図は第1図のA−A′断面視図、第3図は第
1図C−C′断面の拡大視図、第4図は第2図B−
B′断面の拡大視図である。 図において、1……撹拌羽根車、2……容器、
3……入口、4……出口、5……撹拌要素、6…
…容器の内周壁、7……主撹拌羽根、8……副撹
拌羽根である。
FIG. 1 is a main sectional view showing an embodiment of the present invention;
Fig. 2 is a cross-sectional view taken along line A-A' in Fig. 1, Fig. 3 is an enlarged view of cross-section C-C' in Fig. 1, and Fig. 4 is a cross-sectional view taken along line C-C' in Fig. 2.
It is an enlarged view of the B′ section. In the figure, 1... stirring impeller, 2... container,
3... Inlet, 4... Outlet, 5... Stirring element, 6...
...Inner peripheral wall of the container, 7...Main stirring blade, 8...Sub-stirring blade.

Claims (1)

【特許請求の範囲】[Claims] 1 回転する撹拌羽根車1を内蔵する軸心方向が
ほゞ水平に設置される容器2の一端に入口3、他
端に出口4を有し、前記撹拌羽根車1の撹拌要素
5は容器2の内周壁6に沿つて回転外側部位に撹
拌羽根車1の軸心方向に平行な撹拌面Eを有する
主撹拌羽根7群と、該主撹拌羽根7群の内側に位
置して、前記容器2の軸心方向に対し傾斜した送
り面Fを有することが出来る小片状の副撹拌羽根
8群を具備し、前記出口4は前記容器2の壁面に
あつて該容器2の軸心とほゞ同じ高さH付近に設
け、かつ、前記出口4はその開口断面aの下辺b
の水平高さhが上下方向に調節可能にしたことを
特徴とする粉粒体の撹拌装置。
1 A container 2 containing a rotating stirring impeller 1 and installed with its axis substantially horizontal has an inlet 3 at one end and an outlet 4 at the other end, and the stirring element 5 of the stirring impeller 1 is connected to the container 2. A group of 7 main stirring blades having a stirring surface E parallel to the axial direction of the stirring impeller 1 on the outer side of rotation along the inner circumferential wall 6 of the container 2; The outlet 4 is provided on the wall surface of the container 2 and is approximately parallel to the axial center of the container 2. The outlet 4 is provided near the same height H, and the outlet 4 is located at the lower side b of the opening cross section a.
A stirring device for powder and granular material, characterized in that the horizontal height h of the powder is adjustable in the vertical direction.
JP55133891A 1980-09-25 1980-09-25 Stirrer for powdery granule Granted JPS5759622A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55133891A JPS5759622A (en) 1980-09-25 1980-09-25 Stirrer for powdery granule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55133891A JPS5759622A (en) 1980-09-25 1980-09-25 Stirrer for powdery granule

Publications (2)

Publication Number Publication Date
JPS5759622A JPS5759622A (en) 1982-04-10
JPS6333898B2 true JPS6333898B2 (en) 1988-07-07

Family

ID=15115511

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55133891A Granted JPS5759622A (en) 1980-09-25 1980-09-25 Stirrer for powdery granule

Country Status (1)

Country Link
JP (1) JPS5759622A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0634599U (en) * 1992-10-16 1994-05-10 株式会社イナックス Heating toilet seat heater circuit

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4868656B2 (en) * 2001-04-23 2012-02-01 ツカサ工業株式会社 Continuous powder mixing equipment
JP2002336670A (en) * 2001-05-14 2002-11-26 Tsukasa Kogyo Kk Apparatus for blending granular substance

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0634599U (en) * 1992-10-16 1994-05-10 株式会社イナックス Heating toilet seat heater circuit

Also Published As

Publication number Publication date
JPS5759622A (en) 1982-04-10

Similar Documents

Publication Publication Date Title
US4296072A (en) Apparatus for the treatment of wet solids, especially pulpy materials, by heating or cooling
KR100263717B1 (en) Continuous humidification method and apparatus of grain and use of the humidifier
GB2052705A (en) Apparatus for drying and granulating wet pasty and/or fusible materials
US3425135A (en) Rotary solids processing apparatus and method
JPS58501245A (en) Particulate matter treatment
JPS6333898B2 (en)
JP3709499B2 (en) Drying equipment
US2174897A (en) Drying or cooling and aerating apparatus
GB1462794A (en) Granulating apparatus
US1903166A (en) Mill for pulverizing and the like
JP3569131B2 (en) Granulation drying equipment
SU985647A1 (en) Spray dryer for liquid products in fluidized bed of inert bodies
CN210993077U (en) Stirring structure of single-cone crystallization dryer discharge port
CN223619345U (en) A storage device for from type membrane production raw materials
KR930000436A (en) Grinding Mixing Drying Equipment
JP2003287369A (en) Horizontal rotary dryer
JP2004353926A (en) Method of manufacturing dried product
RU50644U1 (en) DRUM DRYER FOR BULK THERMAL SENSITIVE MATERIALS
CN216620595U (en) A centrifuge discharge structure with drying function
JPS598738Y2 (en) Equipment for producing porous dry pellets of adhesive wetting substances
CN220298801U (en) Automatic powder packaging machine
JPS6333072B2 (en)
JPH0771441B2 (en) Powder temperature controller
SU991115A1 (en) Drum for drying agricultural products
JPH0235944A (en) Device for heating treatment of solid or solid-liquid mixture