JPS6250180B2 - - Google Patents

Info

Publication number
JPS6250180B2
JPS6250180B2 JP58197687A JP19768783A JPS6250180B2 JP S6250180 B2 JPS6250180 B2 JP S6250180B2 JP 58197687 A JP58197687 A JP 58197687A JP 19768783 A JP19768783 A JP 19768783A JP S6250180 B2 JPS6250180 B2 JP S6250180B2
Authority
JP
Japan
Prior art keywords
liquid
chamber
overflow
treated
substance
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
JP58197687A
Other languages
Japanese (ja)
Other versions
JPS6090032A (en
Inventor
Katsuhisa Yamanaka
Keishin Furukawa
Masahiko Ishibe
Chikao Oda
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP58197687A priority Critical patent/JPS6090032A/en
Publication of JPS6090032A publication Critical patent/JPS6090032A/en
Publication of JPS6250180B2 publication Critical patent/JPS6250180B2/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
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/625Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis the receptacle being divided into compartments, e.g. with porous divisions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • B01F27/701Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms comprising two or more shafts, e.g. in consecutive mixing chambers
    • B01F27/702Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms comprising two or more shafts, e.g. in consecutive mixing chambers with intermeshing paddles

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、蒸発を伴う粘性物質を連続的に処理
する装置に係り、少量生産用の重合機に好適な混
和機の仕切り構造に関するものである。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to an apparatus for continuously processing a viscous substance accompanied by evaporation, and relates to a partition structure of a mixing machine suitable for a polymerization machine for small-scale production. .

〔発明の背景〕[Background of the invention]

一般に、反応の進行中揮発性物質の除去等の蒸
発を伴う粘性物質の処理においては、減圧下操作
とし、かつ、一端に原料供給口、他端に排出口を
有する横型反応装置を用いて連続的に処理を行う
のが効果的である。この蒸発により除去される揮
発性物質の蒸発量は減圧度に比例して上昇する
が、雰囲気圧力を急激に低下させると、蒸発によ
り除去される揮発性物質と共に粘性物質の一部が
系外へ排出される。したがつて、従来は複数個の
処理装置を直列につなぎ、各処理装置での操作圧
力を順次低下させることにより揮発性物質の除去
が行われていた。
Generally, in the treatment of viscous substances that involve evaporation, such as removal of volatile substances during the reaction, operation is performed under reduced pressure, and a horizontal reactor with a raw material supply port at one end and a discharge port at the other end is used continuously. It is effective to perform the processing in a specific manner. The amount of volatile substances removed by this evaporation increases in proportion to the degree of pressure reduction, but if the atmospheric pressure is suddenly reduced, some of the viscous substances will flow out of the system along with the volatile substances removed by evaporation. be discharged. Therefore, conventionally, volatile substances have been removed by connecting a plurality of processing devices in series and sequentially lowering the operating pressure in each processing device.

このような従来の方法によると処理装置の構成
が複数となり、 (1) 処理工程の複雑化 (2) 装置製作コストの増加 (3) 装置設置スペースの増加 (4) 操作やメンテナンス個所の増加と作業の複雑
化 等の欠点があつた。
Such conventional methods require multiple configurations of processing equipment, resulting in (1) increased complexity of the processing process, (2) increased equipment manufacturing costs, (3) increased equipment installation space, and (4) increased number of operating and maintenance locations. There were drawbacks such as complication of work.

そこで、これらの問題を解決する方法として、
一つの容器を複数の室に仕切り、実質的に複数個
の処理装置を直列につないだと同等の効果を有す
る装置が考案されている。ところが、この装置を
実用に供しようとした時いくつかの問題が生じ、
これらの解決を図る必要がある。すなわち、 (1) 各室の液面は独立に液面調整が可能であるこ
と(隣室の圧力変動に影響されない)。
Therefore, as a way to solve these problems,
An apparatus has been devised in which a single container is partitioned into a plurality of chambers and a plurality of processing apparatuses are connected in series to achieve the same effect. However, when trying to put this device into practical use, several problems arose.
It is necessary to try to resolve these issues. In other words, (1) The liquid level in each chamber can be adjusted independently (not affected by pressure fluctuations in adjacent chambers).

(2) 仕切り部において、液の異常滞留が生じない
こと。
(2) There should be no abnormal accumulation of liquid in the partition.

(3) 仕切り部の構造が簡単で、経済的であるこ
と。等が満足される構造でなければならない。
(3) The structure of the partition should be simple and economical. The structure must satisfy the following.

特に、(1)に記載の液面制御については操作上極
めて重要である。
In particular, the liquid level control described in (1) is extremely important for operation.

現在、1つの容器を仕切り板により複数の室に
仕切り多室構造とした横型粘性物質処理装置が考
案されているが、この仕切り構造は、入口側から
見て被処理物質流路としての切欠きをもつ仕切板
の後方に隣接して溢流板を設けた構造となつてい
る。この場合には、隣接する2室の圧力差により
被処理液の滞留量が変化するため、被処理液の滞
留時間が変動する等の欠点がある。つまり、この
場合の隣り合う2室の圧力差は、1室の液面とそ
の後方の溢流板での溢流液面との液面差とによつ
て補償されるので、溢流板からの溢流路を入口と
する室側の操作圧力が変動すればそれに伴い仕切
板側の液面高さも変動する。そのため、被処理液
の滞留時間が変化することになる。
Currently, a horizontal viscous substance processing device has been devised that has a multi-chamber structure in which one container is partitioned into multiple chambers using partition plates. The structure has an overflow plate adjacent to the rear of the partition plate. In this case, since the amount of the liquid to be treated changes due to the pressure difference between two adjacent chambers, there are drawbacks such as the residence time of the liquid to be treated changes. In other words, the pressure difference between the two adjacent chambers in this case is compensated for by the liquid level difference between the liquid level in one chamber and the overflow liquid level at the overflow plate behind it. If the operating pressure on the chamber side whose inlet is the overflow path changes, the liquid level height on the partition plate side will also change accordingly. Therefore, the residence time of the liquid to be treated changes.

〔発明の目的〕[Purpose of the invention]

本発明は、このような一つの装置内において順
次操作圧力を低下させ多段階の圧力操作を行うの
に際して、操作圧力の変動に影響されることな
く、液滞留量を一定にすることができる仕切り構
造を提供することにある。
The present invention provides a partition that can keep the amount of liquid retained constant without being affected by fluctuations in the operating pressure when performing multi-stage pressure operation by sequentially lowering the operating pressure within such a single device. It's about providing structure.

〔発明の概要〕[Summary of the invention]

本発明は、被処理物質流路としての切欠きのあ
る仕切板を垂直に設け、空間部分を遮断して多室
構造とし、各室毎に減圧度に差を設けて連続的に
粘性物質を処理する装置において、多室構造での
隣り合う2室の圧力差を、1室の液面(溢流板高
さ液面)と隣接して設けられた仕切板との間に生
ずる溢流路での液頭差によつて補償するようにし
たものである。このことにより、各室の操作圧力
が変動した場合でも、隣り合う2室の圧力差はこ
の溢流路での液頭差の変動のみにて確保すること
ができるので、各室での液滞留量(液面)は常に
一定とすることができる。
The present invention creates a multi-chamber structure by vertically installing a partition plate with a notch as a flow path for the substance to be treated, blocking the space, and creating a difference in the degree of pressure reduction in each chamber to continuously transport the viscous substance. In a processing device, the pressure difference between two adjacent chambers in a multi-chamber structure is determined by an overflow channel that occurs between the liquid level in one chamber (overflow plate height liquid level) and a partition plate installed adjacent to the liquid level. This is compensated for by the difference in the liquid head at. As a result, even if the operating pressure of each chamber fluctuates, the pressure difference between two adjacent chambers can be ensured only by the fluctuation of the liquid head difference in this overflow path, so the liquid does not accumulate in each chamber. The amount (liquid level) can always be constant.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を図面を用いて説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.

第1,2図は本発明の一実施例を示したもの
で、1は加熱装置14を設けた外壁、2は被処理
物質の入口、3は被処理物質の出口、4は排出口
を示し、液流路7を持つ仕切板6によつて2室に
分割されている。しかして、被処理物質の入口2
から見て溢流板5の後方に隣接して、溢流板5と
平行に上記仕切板6は設けられており、水平に架
設した撹拌軸10に撹拌羽根11が取付けられて
処理液を撹拌するようにされている。
Figures 1 and 2 show an embodiment of the present invention, where 1 is an outer wall provided with a heating device 14, 2 is an inlet for the substance to be treated, 3 is an outlet for the substance to be treated, and 4 is a discharge port. It is divided into two chambers by a partition plate 6 having a liquid flow path 7. Therefore, the inlet 2 of the substance to be treated
The partition plate 6 is provided adjacent to the rear of the overflow plate 5 and parallel to the overflow plate 5 when viewed from above, and a stirring blade 11 is attached to a horizontally installed stirring shaft 10 to stir the processing liquid. It is made to be.

入口2より供給された処理液は、撹拌羽根11
で撹拌されながら溢流板5より溢れ出し、容器の
空間部を完全に遮断した仕切板6に設けられた液
流路7を通り隣の室へと送られ、該室において第
1室と同様に撹拌されながら出口3を通つて装置
外へと連続的に送り出される。
The processing liquid supplied from the inlet 2 is passed through the stirring blade 11
The liquid overflows from the overflow plate 5 while being stirred, passes through the liquid passage 7 provided in the partition plate 6 that completely blocks off the space of the container, and is sent to the next chamber, where the liquid flows in the same manner as the first chamber. It is continuously sent out of the apparatus through the outlet 3 while being agitated.

各室では、適宜な減圧下の元で被処理物質中の
揮発性物質が排気口4より蒸発除去される。ま
た、各室には処理物質の逆混合を防止する上から
堰12が設けられている。
In each chamber, volatile substances in the substance to be treated are evaporated and removed from the exhaust port 4 under appropriate reduced pressure. Further, each chamber is provided with a weir 12 from above to prevent back mixing of the treated substances.

上記溢流板5と仕切板6との組み合せにより、
隣り合う2室の圧力差は、1室とその後方の溢流
路9の液頭差によつて補償される。これにより、
隣り合う2室の操作圧力が変動しても溢流路9で
の液頭差が変動するのみであるので、各室での液
滞留量(液面8)は変ることなく一定とすること
ができる。ここで、溢流板5での溢流路9の形態
は種々のものが採用でき、被処理液を分割する形
態であればよい。
By the combination of the overflow plate 5 and the partition plate 6,
The pressure difference between two adjacent chambers is compensated by the liquid head difference between one chamber and the overflow path 9 behind it. This results in
Even if the operating pressure of two adjacent chambers changes, only the liquid head difference in the overflow path 9 changes, so the amount of liquid retained in each chamber (liquid level 8) can be kept constant without changing. can. Here, various forms of the overflow channel 9 in the overflow plate 5 can be adopted, and any form that divides the liquid to be treated may be used.

通常、粘性物質を処理する場合、蒸発操作を伴
なうので装置内に処理液を充満させず、装置の上
部は空間となつている。そこで、上記のように仕
切板で多室構造とすると前記空間部分は完全に遮
断しなければならないため、溢流路9での液面は
常に液流路7としての切欠きより上方となるよう
に、各室の被処理物質の滞留状態を管理する必要
がある。なお、液流路7として仕切板6に設けら
れる切欠きの位置、形状、大きさ等について特に
限定はなく、各装置で最適のものを決定すること
ができる。
Normally, when processing a viscous substance, an evaporation operation is involved, so the apparatus is not filled with a processing liquid, and the upper part of the apparatus is left open. Therefore, when creating a multi-chamber structure using partition plates as described above, the space must be completely blocked off, so that the liquid level in the overflow channel 9 is always above the notch serving as the liquid flow channel 7. In addition, it is necessary to control the retention status of the substances to be treated in each chamber. Note that there are no particular limitations on the position, shape, size, etc. of the notch provided in the partition plate 6 as the liquid flow path 7, and the optimum one can be determined for each device.

第3,4図は、液流路7の形状により溢流路9
での液滞流量ができるだけ少なくてすむように、
溢流溝13を設けた本発明の他の実施例を示した
ものである。
3 and 4 show an overflow channel 9 due to the shape of the liquid channel 7.
In order to minimize the amount of liquid stagnant at
This figure shows another embodiment of the present invention in which an overflow groove 13 is provided.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、従来複数個の容器を用いて行
われていた多段圧力処理を一つの容器にて行える
ようになり、操作圧力の変動に影響されることな
く各室での液滞留量を一定とすることができると
いう効果がある。
According to the present invention, multi-stage pressure treatment, which was conventionally performed using multiple containers, can now be performed with a single container, and the amount of liquid retained in each chamber can be controlled without being affected by fluctuations in operating pressure. This has the effect that it can be kept constant.

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

第1図は本発明の一実施例の縦断面図、第2図
は第1図のA−A線断面図、第3図は本発明の他
の実施例の縦断面図、第4図は第3図のB−B線
断面図である。 1……外壁、2……入口、3……出口、4……
排気口、5……溢流板、6……仕切板、7……液
流路、8……液面、9……溢流路、10……撹拌
軸、11……撹拌羽根、12……堰、13……溢
流溝、14……加熱装置。
FIG. 1 is a longitudinal cross-sectional view of one embodiment of the present invention, FIG. 2 is a cross-sectional view taken along the line A-A in FIG. 1, FIG. 3 is a longitudinal cross-sectional view of another embodiment of the present invention, and FIG. FIG. 4 is a sectional view taken along line BB in FIG. 3; 1... Outer wall, 2... Entrance, 3... Exit, 4...
Exhaust port, 5... Overflow plate, 6... Partition plate, 7... Liquid channel, 8... Liquid level, 9... Overflow channel, 10... Stirring shaft, 11... Stirring blade, 12... ...Weir, 13...Overflow groove, 14...Heating device.

Claims (1)

【特許請求の範囲】[Claims] 1 被処理物質流路としての切欠きのある仕切板
を垂直に設け、空間部分を遮断して多室構造と
し、一方に被処理物質の入口を有し他方に出口を
有し、各室に排気口を設けた粘性物質の混和機に
おいて、入口側から見て仕切板の前方に溢流部材
を設けたことを特徴とする混和機の仕切り構造。
1 A partition plate with a notch as a flow path for the substance to be treated is installed vertically, and the space is blocked off to create a multi-chamber structure, with an inlet for the substance to be treated on one side and an outlet on the other side, with each chamber having a A partition structure for a viscous substance mixer provided with an exhaust port, characterized in that an overflow member is provided in front of the partition plate when viewed from the inlet side.
JP58197687A 1983-10-24 1983-10-24 Partition structure of kneader Granted JPS6090032A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58197687A JPS6090032A (en) 1983-10-24 1983-10-24 Partition structure of kneader

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58197687A JPS6090032A (en) 1983-10-24 1983-10-24 Partition structure of kneader

Publications (2)

Publication Number Publication Date
JPS6090032A JPS6090032A (en) 1985-05-21
JPS6250180B2 true JPS6250180B2 (en) 1987-10-23

Family

ID=16378675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58197687A Granted JPS6090032A (en) 1983-10-24 1983-10-24 Partition structure of kneader

Country Status (1)

Country Link
JP (1) JPS6090032A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6253336A (en) * 1985-09-02 1987-03-09 Toyobo Co Ltd Horizontal reactor
JP4607379B2 (en) * 2001-07-13 2011-01-05 住友精化株式会社 Continuous agglomeration apparatus and multistage polymerization apparatus equipped with the same
US7083319B2 (en) 2003-05-15 2006-08-01 Buss Sms Gmbh Verfahrenstechnic Large-volume reactor having a plurality of process spaces
JP6399929B2 (en) * 2012-07-30 2018-10-03 株式会社新日南 Kneading equipment
CN105372098B (en) * 2015-10-28 2017-09-29 浙江省海洋水产研究所 A kind of isolated planktonic organism halving sampling equipment

Also Published As

Publication number Publication date
JPS6090032A (en) 1985-05-21

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