JPH0311299B2 - - Google Patents
Info
- Publication number
- JPH0311299B2 JPH0311299B2 JP25071685A JP25071685A JPH0311299B2 JP H0311299 B2 JPH0311299 B2 JP H0311299B2 JP 25071685 A JP25071685 A JP 25071685A JP 25071685 A JP25071685 A JP 25071685A JP H0311299 B2 JPH0311299 B2 JP H0311299B2
- Authority
- JP
- Japan
- Prior art keywords
- spiral
- stirring
- rod
- processing apparatus
- liquid
- 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
Links
- 238000003756 stirring Methods 0.000 claims description 25
- 239000000126 substance Substances 0.000 claims description 7
- 239000011346 highly viscous material Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 description 26
- 230000000694 effects Effects 0.000 description 7
- 230000003031 feeding effect Effects 0.000 description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- -1 polyethylene terephthalate Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G85/00—General processes for preparing compounds provided for in this subclass
- C08G85/006—Scale prevention in polymerisation reactors
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyesters Or Polycarbonates (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、高粘性物質の連続処理装置に係り、
特にポリエチレンテレフタレート,ポリカーボネ
ートなどの連続縮重合に好適な連続処理装置に関
するものである。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a continuous processing apparatus for highly viscous substances,
In particular, it relates to a continuous processing apparatus suitable for continuous polycondensation of polyethylene terephthalate, polycarbonate, and the like.
一般に、高粘性物質の混練,反応等の連続処理
においては、装置内でのデツドスペースをできる
だけ少なくし、かつ、押し出し流れに近い操作が
要求される。このために横長円筒状の容器を用
い、2本の撹拌翼を長手方向に設置したものが
種々考案されている。例えば、特公昭52−29019
号に示されているように、パドル翼を多段に配列
して容器内面を全てかき取れる構造としてデツド
スペースを少なくしたものがあるが、被処理液が
数千ポイズ以上の高粘度になつた場合には、回転
軸表面に付着した液は共まわりしてスケーリング
等の原因となるなど問題がある。そこで、この回
転軸を無くして、共まわりを少なくする試みがな
され、特公昭49−40732号に提案されているよう
に、一部をくり抜いた円板の外周部を連結して回
転軸を無くしたものがある。これにより、回転軸
での共のまわりは無くなるが、円板状の撹拌翼の
表面に付着した高粘性液は流動しにくく、翼に共
まわりしてスケーリング等の原因となる
〔発明の目的〕
本発明の目的は、このような従来技術の問題点
を解決し、容器内での液の共まわり等によるデツ
ドスペースを十分少なくして、スケーリングなど
を防止し、品質の良い処理物が得られる連続処理
装置を提供することにある。
Generally, in continuous processing such as kneading and reaction of highly viscous substances, it is required to minimize the dead space within the apparatus and to perform operations similar to extrusion flow. For this purpose, various designs have been devised in which a horizontally long cylindrical container is used and two stirring blades are installed in the longitudinal direction. For example, Special Public Interest Publication No. 52-29019
As shown in the issue, there is a structure in which paddle blades are arranged in multiple stages to scrape the entire inner surface of the container to reduce the dead space, but when the liquid to be treated has a high viscosity of several thousand poise or more, However, there is a problem in that the liquid adhering to the surface of the rotating shaft rotates together and causes scaling. Therefore, an attempt was made to eliminate this rotating shaft and reduce the rotation, and as proposed in Japanese Patent Publication No. 49-40732, the outer periphery of a partially hollowed out disk was connected to eliminate the rotating shaft. There is something I did. As a result, there is no co-rotation around the rotating shaft, but the highly viscous liquid attached to the surface of the disc-shaped stirring blade is difficult to flow and co-rotates around the blade, causing scaling etc. [Object of the invention] The purpose of the present invention is to solve the problems of the prior art, to sufficiently reduce the dead space caused by the co-circulation of liquid in the container, to prevent scaling, etc., and to provide a continuous process that allows high-quality processed products to be obtained. The purpose of this invention is to provide a processing device.
本発明は、従来装置での問題点が、回転軸や板
状撹拌翼表面への高粘性液の付着共まわりである
ことに着目してなされたもので、回転軸及び板状
部分を無くし、容器内をくまなくかき取ることが
でき、さらに液の送り効果が得られる棒状構造の
らせん状撹拌翼を持つ高粘性物質連続処理装置を
提案するものである。
The present invention was developed by focusing on the fact that a problem with conventional devices is the adhesion of highly viscous liquids to the rotating shaft and the surface of plate-shaped stirring blades. We propose a continuous processing device for highly viscous substances that has a spiral stirring blade with a rod-like structure that can thoroughly scrape the inside of a container and also provide a liquid feeding effect.
以下、本発明の一実施例を第1図〜第3図によ
り説明する。図において、1は処理装置の容器本
体で、第2図に示す断面を持つ横長円筒状容器で
あり、一般に熱媒ジヤケツト(図示せず)で外周
を覆われている。2は容器本体1の両端に取りつ
けられた回転耳軸で左右いずれか一方の回転耳軸
2は駆動装置(図示せず)に連結されている。こ
の容器本体1両端の回転耳軸2間には棒状部材3
a,3bで互いに接続したらせん状部材4a,4
bで構成した撹拌翼5a,5bが取りつけられて
いる。ここで、らせん状部材4aと4bとは互い
にねじり方向が異なり、回転耳軸2の方向から見
てそれぞれの棒状部材3a,3bがお互いに90度
の位相角を持ち、かつ、一方のらせん状部材4a
が他方の棒状部材3bの回転中心にできるだけ近
接して通過するように保持され、容器本体1内の
液を内側で持ち上げる方向に回転する。また、ら
せん状部材4a,4bの外周端は容器本体1の内
壁面にも十分近接して回転する。この結果、被処
理液は本体1内で撹拌されながら、らせん状部材
4a,4bで本体1長手方向への液送り効果が与
えられる。ここで、回転耳軸2は容器本体1の側
面に固定した軸受6によつて支持される。さらに
7,8はそれぞれ被処理液の入口,出口ノズル、
9は揮発物の出口ノズルである。
An embodiment of the present invention will be described below with reference to FIGS. 1 to 3. In the figure, reference numeral 1 denotes a container body of the processing apparatus, which is an oblong cylindrical container having a cross section shown in FIG. 2, and is generally covered on the outer periphery with a heat medium jacket (not shown). Reference numeral 2 denotes rotary ear shafts attached to both ends of the container body 1, and either the left or right rotary ear shaft 2 is connected to a drive device (not shown). A rod-shaped member 3 is provided between the rotary ear shafts 2 at both ends of the container body 1.
Spiral members 4a, 4 connected to each other at a, 3b
Stirring blades 5a and 5b composed of b are attached. Here, the helical members 4a and 4b have different twisting directions, and the respective rod-like members 3a and 3b have a phase angle of 90 degrees with respect to each other when viewed from the direction of the rotary ear shaft 2, and one spiral Member 4a
is held so as to pass as close as possible to the center of rotation of the other rod-shaped member 3b, and rotates in a direction that lifts the liquid in the container body 1 inside. Further, the outer peripheral ends of the spiral members 4a and 4b rotate sufficiently close to the inner wall surface of the container body 1. As a result, while the liquid to be treated is stirred within the main body 1, the spiral members 4a and 4b provide a liquid feeding effect in the longitudinal direction of the main body 1. Here, the rotary ear shaft 2 is supported by a bearing 6 fixed to the side surface of the container body 1. Furthermore, 7 and 8 are the inlet and outlet nozzles for the liquid to be treated, respectively;
9 is a volatile outlet nozzle.
入口ノズル7から容器本体1内に入つてきた高
粘度の被処理液は、撹拌翼5a,5bにより混合
作用を受けながら、同時に液送り作用を受け、出
口ノズル8の方向に向つて移動し、目的の処理操
作を行なつて出口ノズル8から連続して取り出さ
れる。このとき、撹拌翼5a,5bのらせん状部
材4a,4bの先端が互いに相手側の撹拌翼5
a,5bに入り込みながら回転し、容器本体1内
壁面をくまなくかき取りながら液を出口方向へ送
り、さらに、これらの撹拌,液送り作用が棒状の
構造物で行なわれるので、デツドスペースを十分
少なくするることができる。これにより、従来装
置で問題となつていた回転軸表面や、板状撹拌翼
表面への液の付着,共まわりはほとんど無くな
る。 The highly viscous liquid to be treated that has entered the container body 1 from the inlet nozzle 7 is subjected to a mixing action by the stirring blades 5a and 5b, and at the same time receives a liquid feeding action, and moves toward the outlet nozzle 8. After performing the desired processing operation, it is continuously taken out from the outlet nozzle 8. At this time, the tips of the spiral members 4a and 4b of the stirring blades 5a and 5b are connected to the opposite stirring blade 5.
a, 5b, and rotates while scraping the inner wall surface of the container body 1 to send the liquid toward the outlet.Furthermore, since these stirring and liquid feeding actions are performed by a rod-shaped structure, the dead space is sufficiently reduced. You can. As a result, the adhesion of liquid to the surface of the rotating shaft and the surface of the plate-shaped stirring blade, which has been a problem with conventional devices, and co-rotation are almost eliminated.
本発明の連続処理装置により、ポリエチレンテ
レフタレートやポリカーボネート等の縮重合を行
う場合には、重合反応により被処理液の粘度は数
千ポイズから数万ポイズにより上昇するが、十分
な撹拌作用によりデツドスペースをほとんど無く
することができ、さに良好な表面更新作用が得ら
れて品質の良い重合物を得ることができる。この
とき副性するエチレングリコールなどの揮発物
は、揮発物出口ノズル9より真空装置(図示せ
ず)を経て排出される。このような高粘度液から
の揮発物の除去操作においては、本装置により容
器本体1の内側で液を持ち上げる方向に撹拌翼5
a,5bを回転させることにより、撹拌翼5a,
5bの先端が互いにかみ合つた状態から遠ざかる
際に被処理液に引きちぎり効果を与えるため、表
面更新作用がさらに高められ、揮発物の除去効果
がさらに向上する。 When condensation polymerization of polyethylene terephthalate, polycarbonate, etc. is carried out using the continuous processing apparatus of the present invention, the viscosity of the liquid to be treated increases from several thousand poise to tens of thousands of poise due to the polymerization reaction, but the dead space can be reduced by sufficient stirring action. It is possible to almost eliminate them, obtain a good surface renewal effect, and obtain a high-quality polymer. At this time, volatile substances such as ethylene glycol, which are secondary substances, are discharged from the volatile substance outlet nozzle 9 via a vacuum device (not shown). In such an operation for removing volatile matter from a high viscosity liquid, the stirring blade 5 is moved in the direction of lifting the liquid inside the container body 1 by this device.
By rotating a, 5b, the stirring blades 5a,
Since the tips of the tips 5b have a tearing effect on the liquid to be treated when they move away from the mutually engaged state, the surface renewal effect is further enhanced, and the volatile matter removal effect is further improved.
本発明の推奨される実施例においては、回転耳
軸2,棒状部材3a,3b及びらせん状部材4
a,4bを中空として、内部に熱媒を循環させる
構造することにより、容器本体1壁面からの熱媒
ジヤケツト(図示せず)からの除熱に加えて、反
応熱や撹拌熱を棒状部材3a,3b及びらせん状
部材4a,4b表面から除去することができ、被
処理液の温度を一定に保つて品質を高めることが
できる。 In a preferred embodiment of the invention, a rotary ear shaft 2, rod-like members 3a, 3b and a spiral member 4 are provided.
By making a and 4b hollow and having a structure in which the heating medium is circulated inside, in addition to removing heat from the heating medium jacket (not shown) from the wall surface of the container main body 1, reaction heat and stirring heat are transferred to the rod-shaped member 3a. , 3b and the surfaces of the spiral members 4a, 4b, the temperature of the liquid to be treated can be kept constant and the quality can be improved.
さらに推奨される実施例においては、第4図に
示すように棒状部材3a,3bに代えて棒状部材
10の断面形状を偏平とし、容器本体1長手方向
に対して角度を持たせたもので、これにより被処
理液の容器本体1長手方向への液送り効果をさら
に強めたり、角度を逆向きに取りつけて液送り効
果を緩和するなど、液送り作用を調節することが
できる。 In a further recommended embodiment, as shown in FIG. 4, instead of the rod-like members 3a and 3b, a rod-like member 10 has a flat cross-sectional shape and is angled with respect to the longitudinal direction of the container body 1. Thereby, the liquid feeding effect can be adjusted, such as further strengthening the liquid feeding effect of the liquid to be treated in the longitudinal direction of the container body 1, or reducing the liquid feeding effect by attaching the container in the opposite direction.
さらに他の実施例においては、第5図に示すよ
うにらせん状部材11を3本用い、Y型の棒状部
材12でこれらを連結して撹拌翼を構成し、2本
の撹拌翼のY型棒状部材を互いに60度の位相角を
持たせて配置したものであり、撹拌作用が強めら
れ良好な混合効果が得られる。 In still another embodiment, as shown in FIG. 5, three spiral members 11 are used, and these are connected by a Y-shaped rod member 12 to form a stirring blade, and two stirring blades are arranged in a Y-shape. Rod-shaped members are arranged with a phase angle of 60 degrees from each other, which strengthens the stirring action and provides a good mixing effect.
本発明によれば、容器内での高粘度の被処理液
の回転軸表面,板状撹拌翼面への付着による共ま
わりが無くなり、デツドスペースを十分少なくで
きると共に、液の容器長手方向への送り作用が得
られるので、スケーリングなどによる品質劣化を
防止することができ、品質の良い高粘性物質を連
続して処理することができる。
According to the present invention, co-rotation due to adhesion of a highly viscous liquid to be treated in a container to the rotating shaft surface and plate-shaped stirring blade surface is eliminated, the dead space can be sufficiently reduced, and the liquid can be fed in the longitudinal direction of the container. Since this effect can be obtained, it is possible to prevent quality deterioration due to scaling, etc., and it is possible to continuously process high-quality, high-viscosity substances.
第1図は本発明による高粘性物質連続処理装置
の部分断面平面図、第2図は第1図の−断面
図、第3図は第1図の−断面図、第4図は本
発明の他の実施例を示す棒状部材の部分断面図、
第5図は本発明の更に他の実施例を示す撹拌翼の
斜視図である。
1……容器本体、2……回転耳軸、3a,3b
……棒状部材、4a,4b……らせん状部材、5
……5a,5b……撹拌翼、6……軸受、7……
入口ノズル、8……出口ノズル、9……揮発物出
口ノズル、10……棒状部材、11……らせん状
部材、12……Y型棒状部材。
FIG. 1 is a partial cross-sectional plan view of a high viscosity substance continuous processing apparatus according to the present invention, FIG. 2 is a cross-sectional view at the side of FIG. A partial sectional view of a rod-shaped member showing another embodiment,
FIG. 5 is a perspective view of a stirring blade showing still another embodiment of the present invention. 1... Container body, 2... Rotating ear shaft, 3a, 3b
...Rod-shaped member, 4a, 4b...Spiral-shaped member, 5
...5a, 5b... Stirring blade, 6... Bearing, 7...
Inlet nozzle, 8... Outlet nozzle, 9... Volatile exit nozzle, 10... Bar-shaped member, 11... Spiral member, 12... Y-shaped bar-shaped member.
Claims (1)
ぞれ2本の回転耳軸を並設し、前記各回転耳軸間
に相互にねじり方向の異なるらせん状部材よりな
る撹拌翼をそれぞれ取付け、かつ、相互に相対応
する撹拌翼を軸方向より見て90度の位相角を持た
せて配置し、前記並設した回転耳軸を一方の撹拌
翼のらせん状部材の先端が他方の撹拌翼の回転中
心に近接して通過するように保持せしめたことを
特徴とする高粘性物質連続処理装置。 2 前記らせん状部材を2本のらせん状部材の中
間部分を棒状部材で接続して形成した特許請求の
範囲第1項記載の高粘性物質連続処理装置。 3 前記らせん状部材の棒状部材を偏平断面と
し、かつ、容器本体の長手方向に角度を持たせて
取付けた特許請求の範囲第2項記載の高粘性物質
連続処理装置。[Scope of Claims] 1. A stirring device in which two rotating ear shafts are arranged in parallel at both ends of a horizontally installed cylindrical container, and spiral members having mutually different twisting directions are arranged between the rotary ear shafts. The blades are attached to each blade, and the corresponding stirring blades are arranged with a phase angle of 90 degrees when viewed from the axial direction, and the rotary ear shafts arranged in parallel are connected to the tip of the helical member of one of the stirring blades. A highly viscous substance continuous processing apparatus characterized in that the stirring blade is held so as to pass close to the rotation center of the other stirring blade. 2. The high-viscosity substance continuous processing apparatus according to claim 1, wherein the spiral member is formed by connecting the intermediate portions of two spiral members with a rod-shaped member. 3. The high viscosity substance continuous processing apparatus according to claim 2, wherein the rod-like member of the spiral member has a flat cross section and is attached at an angle in the longitudinal direction of the container body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25071685A JPS62112623A (en) | 1985-11-11 | 1985-11-11 | High viscosity substance continuous processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25071685A JPS62112623A (en) | 1985-11-11 | 1985-11-11 | High viscosity substance continuous processing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62112623A JPS62112623A (en) | 1987-05-23 |
| JPH0311299B2 true JPH0311299B2 (en) | 1991-02-15 |
Family
ID=17211986
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25071685A Granted JPS62112623A (en) | 1985-11-11 | 1985-11-11 | High viscosity substance continuous processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62112623A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0584801A3 (en) * | 1992-08-26 | 1994-09-14 | Mitsubishi Chem Ind | Aromatic polycarbonate resins and process for the preparation thereof |
| US5519106A (en) * | 1992-08-26 | 1996-05-21 | Mitsubishi Chemical Corporation | Process for the preparation of aromatic polycarbonate resins |
| JPH11158262A (en) | 1997-11-28 | 1999-06-15 | Hitachi Ltd | Method for producing polycarbonate |
| US6350848B1 (en) | 1997-11-28 | 2002-02-26 | Hitachi, Ltd. | Process and apparatus for producing polycarbonate |
| US6399739B1 (en) | 2001-08-22 | 2002-06-04 | General Electric Company | Preparation of polycarbonate having a predetermined molecular weight and level of endcapping |
-
1985
- 1985-11-11 JP JP25071685A patent/JPS62112623A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62112623A (en) | 1987-05-23 |
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