JPH0626654B2 - Mixed reaction processor - Google Patents

Mixed reaction processor

Info

Publication number
JPH0626654B2
JPH0626654B2 JP62011176A JP1117687A JPH0626654B2 JP H0626654 B2 JPH0626654 B2 JP H0626654B2 JP 62011176 A JP62011176 A JP 62011176A JP 1117687 A JP1117687 A JP 1117687A JP H0626654 B2 JPH0626654 B2 JP H0626654B2
Authority
JP
Japan
Prior art keywords
processing container
raw material
product
processed
receiving
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 - Lifetime
Application number
JP62011176A
Other languages
Japanese (ja)
Other versions
JPS63178835A (en
Inventor
隆文 嶋田
秀太郎 森
泰起 梶
厳 浜本
節男 大本
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP62011176A priority Critical patent/JPH0626654B2/en
Publication of JPS63178835A publication Critical patent/JPS63178835A/en
Publication of JPH0626654B2 publication Critical patent/JPH0626654B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/84Mixing plants with mixing receptacles receiving material dispensed from several component receptacles, e.g. paint tins
    • B01F33/841Mixing plants with mixing receptacles receiving material dispensed from several component receptacles, e.g. paint tins with component receptacles fixed in a circular configuration on a horizontal table, e.g. the table being able to be indexed about a vertical axis

Landscapes

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は化学工業界,食品,薬品,窯業等の産業分野で
使用される混合反応処理装置、即ち2種以上の原料を混
合するための、又は1種或は2種以上の原料を混合反応
させるための混合反応処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a mixed reaction treatment apparatus used in the industrial fields such as chemical industry, food, chemicals, and ceramics, that is, for mixing two or more raw materials. , Or a mixed reaction treatment device for mixing and reacting one kind or two or more kinds of raw materials.

(従来の技術) 原料を混合器や反応器等の処理容器に供給した後に、加
熱や攪拌等の操作を行いながら一定時間保持して混合や
反応を行わせ、所定時間後に内容物を製品(又は中間製
品)として処理容器から抜出す、所謂バッチ操作装置は
従来より産業界に多数存在する。
(Prior Art) After supplying raw materials to a processing container such as a mixer or a reactor, the materials are kept for a certain period of time while performing operations such as heating and stirring to allow mixing and reaction, and after a predetermined time, the contents are made into products ( There are many so-called batch operating devices in the industrial field, which are called as batch products (or intermediate products) from the processing container.

従来のバッチ操作を行わせる装置には、処理容器に多数
の原料受入口が設けられており、複数の原料が順次供給
される様になっている。また製品(又は中間製品)の抜出
しについては、1種の製品の場合は1個の抜出口で済む
が、通常は多種の製品を同一の処理容器で製造するた
め、製品毎に抜出口を要している。更に処理容器や配管
の清掃を目的として洗浄剤を供給,排出する場合も多用
されているが、この時は更に一対の受入口,抜出口が追
加される場合が多い。この様に従来のバッチ操作用処理
容器には、多数の受入,抜出口が設けられていた。更に
それに接続されているバルブや配管が処理容器の回りに
集中している。
A conventional apparatus for performing a batch operation is provided with a large number of raw material inlets in a processing container so that a plurality of raw materials are sequentially supplied. In addition, with regard to the withdrawal of products (or intermediate products), in the case of one type of product, only one withdrawal outlet is required, but normally various products are manufactured in the same processing container, so an withdrawal outlet is required for each product. is doing. Further, it is often used to supply and discharge the cleaning agent for the purpose of cleaning the processing container and the piping, but in this case, a pair of receiving inlets and outlets are often added. As described above, the conventional processing container for batch operation has a large number of receiving and discharging ports. Furthermore, the valves and pipes connected to it are concentrated around the processing container.

第3図は従来の典型的なバッチ式処理装置を示す。図に
おいて攪拌機101を有する処理容器102の上部には、原料
受入口103a〜e、洗浄用溶剤受入口103fが設けられてお
り、処理容器102の下部には製品抜出口104a,104b及び
洗浄剤の溶剤抜出口104cが設けられている。また各々の
受入,抜出口にはバルブ及び配管が接続されている。
FIG. 3 shows a typical conventional batch type processing apparatus. In the figure, a raw material receiving port 103a-e and a cleaning solvent receiving port 103f are provided in the upper part of a processing container 102 having a stirrer 101, and product lowering port 104a, 104b and a cleaning agent of the cleaning agent are provided in the lower part of the processing container 102. A solvent outlet 104c is provided. A valve and piping are connected to each of the receiving and outlet ports.

そしてこの装置を用いて製品αを製造する場合は、原料
A,B,Cを原料受入口103a,103b,103cから処理容器102
に、各々順次供給し、攪拌しながら(場合によっては壁
面から加熱又は冷却しながら)混合または反応させ、製
品を製品抜出口104aから抜出す。次に溶剤受入口103fか
ら洗浄用溶剤を供給し、処理容器102を洗浄してから溶
剤抜出口104cを用いて溶剤を抜出す。
When the product α is manufactured using this apparatus, the raw materials A, B and C are fed from the raw material inlets 103a, 103b, 103c to the processing container 102.
Are sequentially supplied, and mixed or reacted with stirring (while heating or cooling from the wall surface in some cases) to withdraw the product from the product outlet 104a. Next, a cleaning solvent is supplied from the solvent receiving port 103f to wash the processing container 102, and then the solvent is discharged using the solvent discharging port 104c.

また製品βを製造する場合には、原料A,D,Eを原料受
入口103a,103d,103eから処理容器102に各々順次供給
し、混合等の処理をした後、製品を製品抜出口104bから
抜出す。
When manufacturing the product β, the raw materials A, D, and E are sequentially supplied from the raw material inlets 103a, 103d, and 103e to the processing container 102, and after being processed such as mixing, the product is discharged from the product outlet 104b. Pull out.

以上のように従来のバッチ式処理装置では、複数の原料
を各々の配管,バルブ,受入口を介して処理容器に供給
し、製品はそれぞれの製品毎の抜出口から抜出す方式が
一般的であった。
As described above, in the conventional batch type processing apparatus, it is general that a plurality of raw materials are supplied to the processing container through the respective pipes, valves, and receiving ports, and the product is extracted from the outlet of each product. there were.

(発明が解決しようとする問題点) 前記の従来のバッチ式処理装置には、処理容器に多数の
受入口,抜出口が取り付けられ、更にバルブ,配管が接
続されているため、主要機器である処理容器の周辺が複
雑になり、施工上,操作上困難となるなどの問題があっ
た。また処理容器を加熱,冷却する場合のジャケットの
面積が、受入,抜出口が多数あるため低減し、伝熱面積
の確保上不利となるなどの欠点があった。
(Problems to be Solved by the Invention) In the conventional batch type processing apparatus described above, a large number of inlets and outlets are attached to the processing container, and further valves and pipes are connected, which is a main equipment. There was a problem that the surroundings of the processing container became complicated and it became difficult in terms of construction and operation. Further, the area of the jacket for heating and cooling the processing container is reduced due to the large number of inlets and outlets, which is disadvantageous in securing the heat transfer area.

更に処理容器を常温以外で使用する場合には、受入口,
抜出口が多数あるため放熱面積が大きくなり、熱損失が
大となるなどの欠点があった。また多数設けられている
受入口,抜出口内が、所謂液溜りとなり、製品純度上,
洗浄上,製品収率上において不利となるばかりでなく、
処理容器に高級材質を使用する場合には、受入口,抜出
口まで同質材質とする必要があるため、高コストとなる
などの問題があった。
Furthermore, when the processing container is used at other than room temperature,
Since there are many outlets, there is a drawback that the heat dissipation area is large and the heat loss is large. In addition, the large number of inlets and outlets form so-called liquid pools, which increases product purity.
Not only is it disadvantageous in terms of washing and product yield,
When a high-quality material is used for the processing container, it is necessary to use the same material for the inlet and outlet, which causes a problem such as high cost.

本発明は前記従来の問題点を解決するために提案された
ものである。
The present invention has been proposed to solve the above conventional problems.

(問題点を解決するための手段) このため本発明は、原料受入口と処理物抜出口を有する
処理容器、同処理容器を回転移動させるための回転支柱
及び駆動部、原料を前記処理容器に供給するための固定
された原料供給ノズル、前記処理容器内の処理物を受入
れるための固定された処理物受入ノズルから構成され、
前記処理容器の回転移動により形成される原料受入口及
び処理物抜出口の円軌跡上に、前記原料供給ノズル及び
処理物受入ノズルを各々配置した構成を備え、これを問
題点解決のための手段とするものである。
(Means for Solving Problems) Therefore, according to the present invention, a processing container having a raw material receiving port and a processed material discharge port, a rotating column and a driving unit for rotationally moving the processing container, and a raw material in the processing container. A fixed raw material supply nozzle for supplying, comprising a fixed processed product receiving nozzle for receiving the processed product in the processing container,
A means for solving the problem is provided, in which the raw material supply nozzle and the processed material receiving nozzle are arranged on the circular loci of the raw material receiving port and the processed material outlet formed by the rotational movement of the processing container. It is what

(作用) 原料を混合,反応させて製品を製造する場合には、処理
容器を間欠的に回転移動させながら、原料貯槽から原料
を各々順次、処理容器に供給する。その後一定時間攪拌
して所定の処理を行い、処理容器の内容物を目的の製品
とする。また製品の抜出し時には、処理容器を処理物受
槽の位置に移動させ、処理物抜出口と処理物受入ノズル
を接続させてから、両方のバルブを開放する。
(Operation) When the raw materials are mixed and reacted to produce a product, the raw materials are sequentially supplied from the raw material storage tank to the treatment container while the treatment container is intermittently rotated. After that, the mixture is stirred for a certain period of time to perform a predetermined process, and the content of the processing container is used as a target product. In addition, when the product is taken out, the processing container is moved to the position of the processing product receiving tank, the processing product outlet and the processing product receiving nozzle are connected, and then both valves are opened.

(実施例) 以下、本発明を図面の実施例について説明すると、第1
図及び第2図は本発明の実施例を示すものである。図に
おいて攪拌機1を有する処理容器2の上部には、原料受
入口3がバルブ4,導管5を介して取り付けられてお
り、下部には処理物抜出口6がバルブ7,導管8を介し
て取り付けられている。処理容器2は、支持アーム9及
び回転座10により回転支柱11の回りを回転移動可能な構
造となっている。12は回転駆動部で、回転支柱11に固定
されており、この部材の中にあるゴムローラ又はギヤ等
で回転座10を回転させる。
(Embodiment) The present invention will be described below with reference to embodiments of the drawings.
FIG. 2 and FIG. 2 show an embodiment of the present invention. In the figure, a raw material inlet 3 is attached to the upper part of a processing container 2 having an agitator 1 via a valve 4 and a conduit 5, and a treated product outlet 6 is attached to a lower part via a valve 7 and a conduit 8. Has been. The processing container 2 has a structure in which the support arm 9 and the rotating seat 10 allow the processing container 2 to rotate around a rotating column 11. Reference numeral 12 denotes a rotary drive unit, which is fixed to the rotary column 11, and rotates the rotary seat 10 by a rubber roller, a gear or the like in this member.

また処理容器2の回転移動により形成される原料受入口
3及び処理物抜出口6の円軌跡上に、複数個の原料供給
ノズル13及び1個又は複数個の処理物受入ノズル14が配
置されている。原料供給ノズル13はバルブ15,導管16を
介して原料貯槽17に連結されており、処理物受入ノズル
14は、バルブ18,導管19を介して処理物受槽20に連結さ
れている。また回転支柱11,原料貯槽17及び処理物受槽
20は、架構21に固定されている。更に原料供給ノズル13
と原料受入口3との間隔、及び処理物受入ノズル14と処
理物抜出口6との間隔は、上下方向に近接しており、水
平方向の位置が一致すれば、ほぼ接続された状態とな
る。また完全な接続を要する場合は、接続用治具により
それを達成することも可能である。
Further, a plurality of raw material supply nozzles 13 and one or a plurality of treated material receiving nozzles 14 are arranged on a circular locus of the raw material inlet 3 and the treated material outlet 6 formed by the rotational movement of the processing container 2. There is. The raw material supply nozzle 13 is connected to a raw material storage tank 17 via a valve 15 and a conduit 16, and is a processed material receiving nozzle.
Reference numeral 14 is connected to a treated material receiving tank 20 via a valve 18 and a conduit 19. In addition, rotating column 11, raw material storage tank 17 and processed material storage tank
20 is fixed to frame 21. Further raw material supply nozzle 13
The distance between the raw material inlet 3 and the raw material receiving port 3 and the distance between the processed material receiving nozzle 14 and the processed material outlet 6 are close to each other in the vertical direction, and if the horizontal positions match, they are almost connected. . If a perfect connection is required, it can be achieved by a connecting jig.

第2図は第1図の平面図を示しており、処理容器2,原
料貯槽17,処理物受槽20,原料供給ノズル13,処理物受
入ノズル14の平面での位置関係のみ図示している。また
回転中心21を中心として処理容器2が回転すると、原料
受入口3及び処理物抜出口6は、軌跡22及び軌跡23を各
各描いて移動する。軌跡22上に原料供給ノズル13a,13b,
13c,13d,13eを設け、軌跡23上に処理物受入ノズル14
α,14β,14γを設けている。
FIG. 2 is a plan view of FIG. 1, and shows only the positional relationship in the plane of the processing container 2, the raw material storage tank 17, the processed material receiving tank 20, the raw material supply nozzle 13, and the processed material receiving nozzle 14. Further, when the processing container 2 rotates about the rotation center 21, the raw material receiving port 3 and the processed material outlet 6 respectively move along a locus 22 and a locus 23. Raw material supply nozzles 13a, 13b,
13c, 13d, and 13e are provided, and the workpiece receiving nozzle 14 is provided on the track 23.
α, 14β and 14γ are provided.

次に以上の如く構成された実施例について作用を説明す
ると、原料A,B,Cを混合,反応させて製品αを製造す
る場合には、処理容器2を間欠的に回転移動させながら
原料貯槽17a,17b,17cから原料A,B,Cを各々順次、処
理容器2に供給する。なお、その時のバルブ操作につい
ての記述は省略する。その後一定時間攪拌して所定の処
理を行い、処理容器2の内容物を目的の製品とする。ま
た製品の抜出し時には、処理容器2を処理物受槽20αの
位置に移動させ、処理物抜出口6と処理物受入ノズル14
αを接続させてから両方のバルブを開放する。
Next, the operation of the embodiment configured as described above will be described. When the raw materials A, B and C are mixed and reacted to produce the product α, the raw material storage tank is intermittently rotated while moving the processing container 2. Raw materials A, B, and C are sequentially supplied to the processing container 2 from 17a, 17b, and 17c. The description of the valve operation at that time is omitted. After that, stirring is performed for a certain period of time to perform a predetermined process, and the content of the processing container 2 is made into a target product. Further, when the product is taken out, the processing container 2 is moved to the position of the processed product receiving tank 20α, and the processed product outlet 6 and the processed product receiving nozzle 14 are provided.
After connecting α, open both valves.

また処理容器2及びその周辺の接液部を洗浄する場合に
は、原料貯槽17eの位置に処理容器2を移動して洗浄溶
剤を受入れ、攪拌洗浄する。この後処理容器2を処理物
受槽20γの位置に移動し、洗浄剤の溶剤を処理物受槽20
γ内に抜出す。また原料貯槽17b,17c,17dに仕込まれて
いる原料B,C,Dから製品βを製造し、処理物受槽20β
に抜出す場合も前述と同様の操作で行える。なお、本実
施例では、原料貯槽17及び処理物受槽20の数を各々5
個,3個としているが、この数に限定されるものではな
く、多品種の原料から多品種の製品を製造する場合に
は、原料貯槽及び処理物槽の数も多くすることができ
る。
Further, when cleaning the processing container 2 and the liquid contact portion around the processing container 2, the processing container 2 is moved to the position of the raw material storage tank 17e, the cleaning solvent is received, and stirring cleaning is performed. After this, the post-treatment container 2 is moved to the position of the treated substance receiving tank 20γ, and the solvent of the cleaning agent is moved to the treated substance receiving tank 20γ.
Extract into γ. In addition, the product β is manufactured from the raw materials B, C, D charged in the raw material storage tanks 17b, 17c, 17d, and the processed product receiving tank 20β
The same operation as described above can also be performed when extracting to. In the present embodiment, the number of raw material storage tanks 17 and the number of processed product receiving tanks 20 are each 5
However, the number of raw material storage tanks and processed product tanks can be increased in the case of manufacturing a wide variety of products from a wide variety of raw materials.

(発明の効果) 以上詳細に説明した如く本発明は構成されているので、
従来の処理容器に取り付けられていたような多数の原料
受入口,処理物抜出口に起因する多くの問題点は完全に
解決される。また回転支柱を中心として、原料受入口,
処理物抜出口が円軌跡で移動するため、原料供給ノズ
ル,処理物受入ノズルとの接続が容易、かつ正確に行え
る。更に多種の原料から多種の製品を製造するのに、本
発明では1基の装置で行えるので操作も容易であり、熱
損失も少なく、かつ原料選択の自由度も高く、柔軟性に
富んだ装置とすることができる。
(Effects of the Invention) Since the present invention is configured as described in detail above,
Many problems caused by a large number of raw material inlets and processed product outlets, which are attached to conventional processing vessels, are completely solved. In addition, the raw material inlet,
Since the processed material outlet moves in a circular path, the connection with the raw material supply nozzle and the processed material receiving nozzle can be performed easily and accurately. Further, even if various products are manufactured from various raw materials, the present invention can be performed with a single device, so that the operation is easy, the heat loss is small, and the flexibility of raw material selection is high, and the device is highly flexible. Can be

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

第1図は本発明の実施例を示す装置の正面断面図、第2
図は同平面図、第3図は従来のバッチ式処理装置を示す
正面断面図である。 図の主要部分の説明 1……攪拌機、2……処理容器 3……原料受入口、6……処理物抜出口 11……回転支柱、12……駆動部 13……原料供給ノズル 14……処理物受入ノズル
1 is a front sectional view of an apparatus showing an embodiment of the present invention, FIG.
FIG. 3 is a plan view of the same, and FIG. 3 is a front sectional view showing a conventional batch type processing apparatus. Description of main parts of the figure 1 ... Stirrer, 2 ... Processing container 3 ... Raw material receiving port, 6 ... Processed material discharge port 11 ... Rotating column, 12 ... Driving part 13 ... Raw material supply nozzle 14 ... Processed material receiving nozzle

───────────────────────────────────────────────────── フロントページの続き (72)発明者 浜本 厳 広島県広島市西区観音新町4丁目6番22号 三菱重工業株式会社広島製作所内 (72)発明者 大本 節男 広島県広島市西区観音新町4丁目6番22号 三菱重工業株式会社広島研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor, Mr. Gen Hamamoto, 4-6-22 Kannon Shinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture Mitsubishi Heavy Industries, Ltd. Hiroshima Works (72) Inventor, Setsuo Omoto 4 Kannon Shinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture 6-22 No. 6 Hiroshima Research Laboratory, Mitsubishi Heavy Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】原料受入口と処理物抜出口を有する処理容
器、同処理容器を回転移動させるための回転支柱及び駆
動部、原料を前記処理容器に供給するための固定された
原料供給ノズル、前記処理容器内の処理物を受入れるた
めの固定された処理物受入ノズルから構成され、前記処
理容器の回転移動により形成される原料受入口及び処理
物抜出口の円軌跡上に、前記原料供給ノズル及び処理物
受入ノズルを各々配置したことを特徴とする混合反応処
理装置。
1. A processing container having a raw material receiving port and a processed material discharge port, a rotating column and a driving part for rotating the processing container, a fixed raw material supply nozzle for supplying the raw material to the processing container, The raw material supply nozzle is formed of a fixed processed material receiving nozzle for receiving the processed material in the processing container, and the raw material supply nozzle is provided on a circular locus of a raw material receiving port and a processed product outlet formed by rotational movement of the processing container. And a processed product receiving nozzle, respectively.
JP62011176A 1987-01-20 1987-01-20 Mixed reaction processor Expired - Lifetime JPH0626654B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62011176A JPH0626654B2 (en) 1987-01-20 1987-01-20 Mixed reaction processor

Applications Claiming Priority (1)

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JP62011176A JPH0626654B2 (en) 1987-01-20 1987-01-20 Mixed reaction processor

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JPS63178835A JPS63178835A (en) 1988-07-22
JPH0626654B2 true JPH0626654B2 (en) 1994-04-13

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JP62011176A Expired - Lifetime JPH0626654B2 (en) 1987-01-20 1987-01-20 Mixed reaction processor

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CN108940085A (en) * 2018-08-07 2018-12-07 南通大学附属医院 A kind of medical treatment and nursing medicament shaking device

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JPS63178835A (en) 1988-07-22

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